Patents
Literature
Hiro is an intelligent assistant for R&D personnel, combined with Patent DNA, to facilitate innovative research.
Hiro

31 results about "Tetrachloropropylene" patented technology

Process

Disclosed is a process for preparing a highly pure 1,1,1,2,3-pentachloropropane product. The method comprises 1-a) providing a reaction mixture comprising ethylene, carbon tetrachloride and a catalyst in a principal alkylation zone to produce 1,1,1,3-tetrachloropropane in the reaction mixture; 1-b) treating the reaction mixture obtained in step 1-a) to obtain a 1,1,1,3-tetrachloropropane feedstock; 2-a) contacting the 1,1,1,3-tetrachloropropane feedstock with a catalyst in a dehydrochlorination zone to produce a reaction mixture comprising 1,1,1,3-tetrachloropropane and 1,1,3-trichloropropene; 2-b) treating the reaction mixture obtained in step 2-a) to obtain a 1,1,3-trichloropropene feedstock; 3-a) contacting the 1,1,3-trichloropropene feedstock with chlorine in a reaction zone to produce a reaction mixture containing 1,1,1,2,3-pentachloropropane and 1,1,3-trichloropropene, the reaction zone being different from the dehydrochlorination zone; and 3-b) treating the reaction mixture obtained in step 3-a) to obtain the highly pure 1,1,1,2,3-pentachloropropane product.
Owner:SPOLEK PRO CHEMICKOU A HUTNI VYROBU

Preparation method for 3,3,3-trifluoropropene

The invention discloses a preparation method for 3,3,3-trifluoropropene, and the preparation method comprises the following steps of: (1) taking carbon tetrachloride and ethylene as a raw material and organic peroxides as a catalyst, and reacting to prepare 1,1,1,3-tetrachloropropane, wherein the molar ratio of carbon tetrachloride and ethylene is (1:1)-(30:1), the reaction pressure is 0.3-1.5MPa, the reaction temperature is 50-150DEG C, and the reaction time is 2-5 hours; (2) taking the prepared 1,1,1,3-tetrachloropropane and anhydrous hydrogen fluoride as a raw material, and preparing 1,1,1-trifluoro-3-chloropropane in a reactor under the action of the catalyst and a polymerization inhibitor, wherein the molar ratio of 1,1,1,3-tetrachloropropane and anhydrous hydrogen fluoride is (1:3)-(1:50), the reaction pressure is 0.2-0.7MPa, the reaction temperature is 40-70DEG C, and the reaction time is 6-8 hours; and (3) carrying out dehydrochlorination on the prepared 1,1,1-trifluoro-3-chloropropane so as to prepare 3,3,3-trifluoropropene.
Owner:衢州环新氟材料有限公司

Process for the production of chlorinated propanes

Processes for the production of chlorinated propanes are provided. The processes comprise catalyzing the chlorination of 1,1,1,3-tetrachloropropane with aluminum chloride, either alone or in combination with ferric chloride. Low intensity conditions are appropriate for the process, e.g., temperatures of from ambient to 100° C. and pressures of from ambient to 200 psig may be used. Even though low intensity conditions are used, the aluminum chloride provides at least 1.5 times greater the conversion rate and / or productivity of 1,1,1,3-tetrachloropropane as compared to ferric chloride when used as a single catalyst under similar processing conditions.
Owner:BLUE CUBE IP

Catalyst for synthesizing 2-chloro-3,3,3-trifluoropropene from 1,1,2,3-tetrachloropropylene and preparation method thereof

The invention relates to a catalyst for synthesizing 2-chloro-3,3,3-trifluoropropene from 1,1,2,3-tetrachloropropylene and a preparation method thereof. The catalyst is composed of Cr, Al and M fluoride, wherein M is one or both of Zn and Co; the Cr-Al-M mol ratio is 1:(0.05-0.2):(0.02-0.1). The preparation method comprises the following steps: adding a KOH alkaline solution into proportional Cr compound, Al compound and M compound to form a precipitate, or directly mechanically blending the three compounds to form a mixture; adding a sucrose-citric acid solution (the sucrose-citric acid mol ratio is 1:1) into the mixture, thoroughly mixing, drying, and roasting in an N2 atmosphere to obtain an oxide containing a carbon template; and treating the oxide precursor containing carbon template with inert gas and anhydrous hydrogen fluoride, and oxidizing in an oxygen atmosphere to remove the template, thereby obtaining the catalyst. The catalyst provided by the invention has the advantages of simple technique, high activity, high selectivity, high stability and the like, and is convenient to produce.
Owner:ZHEJIANG SANMEI CHEM IND

Continuous production method of 1,1,1,3-tetrachloropropane

The invention discloses a continuous production method of 1,1,1,3-tetrachloropropane, wherein the method comprises the steps: (1) under the action of a main catalyst, preheating a mixture of carbon tetrachloride and a cocatalyst, and simultaneously and continuously introducing the preheated mixture and ethylene into a reactor for telomerization reaction to obtain a reaction product; (2) feeding the reaction product obtained in the step (1) into a first vacuum distillation tower, and separating to obtain tower top fraction and tower bottom liquid; and (3) separating the tower bottom liquid obtained in the step (2) in a second vacuum distillation tower to obtain a 1,1,1,3-tetrachloropropane product and a high-boiling residue. The method has the advantages that the process is simple and environmentally friendly, the catalyst does not need to be independently activated, and totally-enclosed integrated continuous production is achieved.
Owner:NINGBO JUHUA CHEM TECH CO LTD

Processes for Producing Chlorinated Hydrocarbons and Methods for Recovering Polyvalent Antimony Catalysts Therefrom

The preparation of chlorinated hydrocarbons, such as pentachloropropanes, such as 1,1,1,2,3-pentachloropropane, from tetrachloropropanes, such as 1,1,1,3-tetrachloropropane, in the presence of a polyvalent antimony compound that includes a pentavalent antimony compound, such as antimony pentachloride, is described. Also described are methods for preparing optionally chlorinated alkenes, such as, tetrachloropropenes, from chlorinated alkanes, such as pentachloropropanes, in the presence of polyvalent antimony compound that includes a pentavalent antimony compound, as well as methods for recovering polyvalent antimony compounds from such processes.
Owner:EAGLE US 2 LLC

Preparation method of 1, 3-dichloro-1, 1-difluoropropane

The invention discloses a preparation method of 1, 3-dichloro-1, 1-difluoropropane, and belongs to the technical field of fluorine-containing chemicals. Under the action of a lewis acid catalyst, in the presence or absence of a solvent, 1, 1, 1, 3-tetrachloropropane reacts with antimony trifluoride to generate 1, 3-dichloro-1, 1-difluoropropane, and the lewis acid catalyst is niobium pentachloride, tantalum pentachloride or antimony pentachloride. According to the preparation method of the 1, 3-dichloro-1, 1-difluoropropane, the raw materials are easy to obtain, the conversion rate is high, the 1, 3-dichloro-1, 1-difluoropropane can be prepared with high selectivity, and the selectivity can reach 90% under better conditions.
Owner:ZHEJIANG FLUORINE CHEM NEW MATERIAL

Method for synthesizing 2,3,3,3-tetrafluoropropene

The invention discloses a method for synthesizing 2,3,3,3-tetrafluoropropene and belongs to the field of organic synthesis. The method comprises the following steps: (1) preparing 2-chloropropene from 1,2-dichloropropane, which serves as a raw material, through continuous catalytic cracking by adopting a fixed bed in the presence of beta-zeolite, which serves as a catalyst; (2) selectively chlorinating 2-chloropropene with chlorine gas under the catalysis of ferric chloride, so as to prepare 2,3,3,3-tetrachloropropylene; and (3) fluorating 2,3,3,3-tetrachloropropylene with hydrofluoric acid under the catalysis of SbF3 or SbF5, thereby obtaining 2,3,3,3-tetrafluoropropene. The synthesis route has the advantages that the source of raw materials is wide, the cost is low, and the product yield is high; and the obtained product can serve as an automotive air conditioning refrigerant and has a positive significance in reduction of greenhouse effect.
Owner:山东联创产业发展集团股份有限公司

Co-production method and device for 3, 3, 3-trifluoropropene and 2-chloro-3, 3, 3-trifluoropropene

The invention relates to a co-production method and device for 3, 3, 3-trifluoropropene and 2-chloro-3, 3, 3-trifluoropropene. The device used in the method comprises a reaction system, a rectification pre-separation system and an azeotrope-like substance extraction separation system. The raw material premixer adopts a falling film evaporation premixer, so that the liquid materials 1, 1, 1, 3-tetrachloropropane are promoted to be quickly and fully vaporized, and meanwhile, the mixing effect of each gas-phase material is enhanced. The rectification pre-separation system adopts a three-tower continuous rectification mode to realize efficient separation of reaction by-products hydrogen chloride, high-boiling residues and excessive hydrogen fluoride. And the azeotrope-like substance extractionand separation system is used for realizing liquid-liquid two-phase extraction and separation of azeotrope-like substances. The production method provided by the invention is realized through the production device with the specific structure and connection relationship, has the advantages of mild reaction conditions, high reaction rate, good atom economy, stable product quality, adjustable product proportion and the like, can realize full-flow automatic control, saves labor, and is suitable for industrial co-production of 3, 3, 3-trifluoropropene and 2-chloro-3, 3, 3-tetrafluoropropene.
Owner:新元化学(山东)股份有限公司 +1

Device and process for preparing 1,1,1,3-tetrachloropropane

The invention discloses a reaction device for preparing 1,1,1,3-tetrachloropropane. The reaction device comprises a reaction kettle, wherein an ethylene circulating system is arranged outside the reaction kettle, a gas distributor is arranged at the bottom of the reaction kettle, the ethylene circulating system comprises an ethylene extraction pipe arranged at the upper portion of the reaction kettle, an ethylene press-in pipe arranged at the lower portion of the reaction kettle, and an ethylene compressor arranged between the ethylene extraction pipe and the press-in pipe, and the ethylene press-in pipe is communicated with the gas distributor. The invention also discloses a process for preparing 1,1,1,3-tetrachloropropane by utilizing the reaction device to react carbon tetrachloride with ethylene. By adopting the process provided by the invention, the generation amount of colloidal oily by-products in the process of preparing 1,1,1,3-tetrachloropropane by reacting carbon tetrachloride with ethylene is reduced, the selectivity of the main product 1,1,1,3-tetrachloropropane is improved, the reaction kettle does not need a stirring device, and the pressure of ethylene in the reaction kettle is reduced at a similar reaction rate.
Owner:浙江佳汇新材料有限公司 +1

Preparation method of 1,1,1,3-tetrachloropropane

The invention discloses a preparation method of 1,1,1,3-tetrachloropropane, which comprises the following steps: mixing carbon tetrachloride with an assistant, preheating, carrying out forced circulation for a period of time, carrying out forced circulation reaction with ethylene in an enhanced reactor to obtain a 1,1,1,3-tetrachloropropane crude product, and carrying out vacuum distillation separation to obtain 1,1,1,3-tetrachloropropane. The method is simple in process and low in energy consumption; the reaction process is easy to control; ethylene, carbon tetrachloride and the assistant obtained at the tower top of the first rectifying tower and 75-95% of residual liquid in the tower bottom of the second rectifying tower can be recycled, the material utilization rate is high, less wasteis generated, the purity of the prepared target product is high, meanwhile, ammonia-nitrogen-free and phosphorus-free catalysts are used, the pollution problem of nitrogen-containing and phosphorus-containing three wastes is solved, and high efficiency and environmental protection are achieved.
Owner:常州新东化工发展有限公司

Gamma-aluminum oxide modified catalyst, preparation method thereof and application of gamma-aluminum oxide modified catalyst in synthesis of 1, 1, 3-trichloropropene

The invention discloses a gamma-aluminum oxide modified catalyst, a preparation method thereof and application of the gamma-aluminum oxide modified catalyst in synthesis of 1, 1, 3-trichloropropene, and belongs to the field of catalyst preparation and organic synthesis. The catalyst takes gamma-aluminum oxide as a carrier and is modified by ferrous chloride and polyethylene glycol to obtain the gamma-aluminum oxide modified catalyst. The application method comprises the following steps: loading the modified catalyst into a tubular reactor, carrying out nitrogen gas activation, under heating condition, introducing 1, 1, 1, 3-tetrachloropropane continuously, so that continuously obtaining of 1, 1, 3-trichloropropene at the tail end of a reaction tube is realized. The modified gamma-aluminumoxide catalyst is used for preparing 1, 1, 3-trichloropropene from 1, 1, 1, 3-tetrachloropropane, has the advantages of being high in efficiency, good in stability and capable of being continuously used for a long time, and has the potential of further enlarged production.
Owner:DALIAN JOIN KING FINE CHEM CO LTD

A method and equipment for clean and environmentally friendly production of 1,1',2,3-tetrachloropropene

The invention discloses a clean and environment-friendly method for producing 1,1',2,3-tetrachloropropene, comprising the following steps: under the premise of nitrogen pressure protection, adding carbon tetrachloride, chlorine Ethylene, and use the catalyst, co-catalyst to catalyze the reaction to obtain the mixture; put the above mixture in the No. With the mol ratio of nitrogen, catalytic reaction obtains tetrachloropropene mixture; With above-mentioned tetrachloropropene mixture, in No. three autoclaves, with FeFeCl 3 As a catalyst, the product 1,1',2,3-tetrachloropropene is obtained by controlling the reaction temperature. The invention also discloses special equipment. The technological process of the present invention is simple, the equipment requirement is relatively low, and is beneficial to industrialization promotion.
Owner:安庆市华璞环保材料科技有限责任公司

One-pot method for preparing 1,1,1,2,3-pentachloropropane with high selectivity and high yield

The invention provides a method for preparing 1,1,1,2,3-pentachloropropane with high selectivity and high yield in a one-pot method. The method uses 1,1,1,3-tetrachloropropane as a raw material to remove Hydrogen chloride reaction to obtain 1,1,3-trichloropropene, when the content of 1,1,3-trichloropropene in the system reaches 4-20%, feed chlorine to react, after feeding chlorine, control 1,1, The content of 3-trichloropropene is 1-6%. When the content of 1,1,1,2,3-pentachloropropane generated in the system reaches 90-99%, stop the reaction. The present invention utilizes a one-pot method to prepare 1,1,1,2,3-pentachloropropane, by controlling the content of 1,1,3-trichloropropene in the system after the dehydrochlorination reaction and introducing chlorine gas, and controlling the generated The control of the content of 1,1,1,2,3-pentachloropropane can greatly reduce side reactions and improve the selectivity and yield of preparing 1,1,1,2,3-pentachloropropane.
Owner:JIANGXI TIANYU CHEM CO LTD

A method for continuously synthesizing 2,3,3,3-tetrafluoropropene in gas phase

The invention discloses a method for continuously synthesizing 2,3,3,3-tetrafluoropropene in a gas phase. In the presence of a catalyst, tetrachloroethylene and methyl chloride undergo a telomerization reaction to generate 1,1,1,2, Catalyzed fluorination of 2‑pentachloropropane and 2,3,3,3‑tetrachloropropene, ,1,1,2,2‑pentachloropropane and 2,3,3,3‑tetrachloropropene to 1,1 ,1,2,2-Pentafluoropropane and 2-Chloro-1,1,1,2-Tetrafluoropropane, 1,1,1,2,2-Pentafluoropropane and 2-Chloro-1,1,1 ,2-Tetrafluoropropane Catalytic Dehydrohalogenation to Prepare 2,3,3,3-Tetrafluoropropene. The invention adopts a continuous method for reaction, the raw materials are economical and easy to obtain, and the reactions of each step are carried out in a reactor, the reaction conditions are easy to control, and the equipment operation is simple; and the conversion rate of each step of the preparation method is better, and the yield of the target product is higher , low equipment investment cost and other advantages, has a wide range of industrial application prospects.
Owner:ZHEJIANG SANMEI CHEM IND

Process for Preparing R-1234yf by Base Mediated Dehydrohalogenation

The invention relates to a process for preparing 2,3,3,3-tetrafluoropropene (CF3CF═CH2), performed using the steps of dehydrohalogenating 1,1,1,2,2-pentafluoropropane (CH3CF2CF3, HFC-245ca) 1,1,1,2-tetrafluoro-2-chloropropane, 1,1,1,2,3-pentafluoropropane (CH2FCHFCF3, HFC-245eb) and / or 1,1,1,2-tetrafluoro-3-chloropropane in the presence of a base, and converting a trifluorodichloropropane or a difluorotrichloropropane or a fluorotetrachloropropane to CH3CF2CF3, 1,1,1,2-tetrafluoro-2-chloropropane, CH2FCHFCF3, and / or 1,1,1,2-tetrafluoro-3-chloropropane.
Owner:MEXICHEM AMANCO HLDG DE C V

Compositions and methods for an integrated 2,3,3,3-tetrafluoropropene manufacturing process

A method of synthesizing 3,3,3-trifluoropropene including contacting 1,3,3,3-tetrachloropropane, in the vapor phase, at a temperature sufficient to effect dehydrochlorination to form 1,1,3-trichloro-1-propene. The 1,1,3-trichloro-1-propene is isolated and subsequently contacted, in the vapor phase, with hydrogen fluoride in the presence of a fluorination catalyst at a temperature sufficient to effect formation of 3,3,3-trifluoropropene.
Owner:THE CHEMOURS CO FC LLC

Compositions and methods for an integrated 2,3,3,3-tetrafluoropropene manufacturing process

A method of synthesizing 3,3,3-trifluoropropene including contacting 1,3,3,3-tetrachloropropane, in the vapor phase, at a temperature sufficient to effect dehydrochlorination to form 1,1,3-trichloro-1-propene. The 1,1,3-trichloro-1-propene is isolated and subsequently contacted, in the vapor phase, with hydrogen fluoride in the presence of a fluorination catalyst at a temperature sufficient to effect formation of 3,3,3-trifluoropropene.
Owner:THE CHEMOURS CO FC LLC

Preparation method of 1, 1, 1, 3-tetrachloropropane

The invention discloses a preparation method of 1, 1, 1, 3-tetrachloropropane, which comprises the following steps: in the presence of a first catalyst and a second catalyst, reacting raw materials containing carbon tetrachloride and ethylene to obtain the 1, 1, 1, 3-tetrachloropropane, the first catalyst comprises a carrier and an active component loaded on the carrier; the active component comprises nano zero-valent iron; the second catalyst comprises an ester compound. According to the preparation method, the supported iron catalyst is adopted, so that the problem of easy agglomeration when pure commercially available iron powder is used as the catalyst can be remarkably improved, the specific surface area of iron is increased, and the reaction is facilitated.
Owner:NINGBO INST OF MATERIALS TECH & ENG CHINESE ACADEMY OF SCI

A co-production method and device for 3,3,3-trifluoropropene and 2-chloro-3,3,3-trifluoropropene

The invention relates to a co-production method and device for 3,3,3-trifluoropropene and 2-chloro-3,3,3-trifluoropropene. The device used in the method includes a reaction system, a rectification pre-separation system, There are three parts in the azeotrope-like extraction and separation system; the raw material pre-mixer adopts a falling-film evaporation pre-mixer to promote the rapid and full vaporization of the liquid material 1,1,1,3-tetrachloropropane, and at the same time, strengthen the mixing effect of each gas phase material. The rectification pre-separation system adopts the three-tower continuous rectification method to realize the efficient separation of reaction by-product hydrogen chloride, high boilers and excess hydrogen fluoride. The azeotrope-like extraction and separation system realizes the liquid-liquid two-phase extraction and separation of azeotrope-like substances. The production method provided by the present invention is realized by the production device with the above-mentioned specific structure and connection relationship, and has the advantages of mild reaction conditions, high reaction rate, good atom economy, stable product quality, adjustable product ratio, etc., and can realize automatic control of the whole process , labor-saving, suitable for industrial co-production of 3,3,3-trifluoropropene and 2-chloro-3,3,3-trifluoropropene.
Owner:新元化学(山东)股份有限公司 +1
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Patsnap Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Patsnap Eureka Blog
Learn More
PatSnap group products