CN114920622B - Technological method for preparing pentafluorobromide benzene - Google Patents

Technological method for preparing pentafluorobromide benzene Download PDF

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CN114920622B
CN114920622B CN202210154859.2A CN202210154859A CN114920622B CN 114920622 B CN114920622 B CN 114920622B CN 202210154859 A CN202210154859 A CN 202210154859A CN 114920622 B CN114920622 B CN 114920622B
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reaction
benzene
pentafluorobromide
crude product
temperature
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CN114920622A (en
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张同斌
姜殿平
刘英亮
王涛
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Zhongtong Technology Dalian Co ltd
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C17/00Preparation of halogenated hydrocarbons
    • C07C17/093Preparation of halogenated hydrocarbons by replacement by halogens
    • C07C17/10Preparation of halogenated hydrocarbons by replacement by halogens of hydrogen atoms
    • C07C17/12Preparation of halogenated hydrocarbons by replacement by halogens of hydrogen atoms in the ring of aromatic compounds
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C17/00Preparation of halogenated hydrocarbons
    • C07C17/38Separation; Purification; Stabilisation; Use of additives
    • C07C17/383Separation; Purification; Stabilisation; Use of additives by distillation

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  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The invention discloses a process method for preparing pentafluorobromide benzene, and belongs to the technical field of fine chemical engineering. The dibromohydantoin is activated in sulfuric acid to bromine the p-pentafluorobenzene to obtain the pentafluorobrominated benzene. The yield of the crude product of the process reaches more than 97 percent, the yield after rectification reaches 95 percent, and the purity is more than 99 percent. The technical scheme of the process has the remarkable characteristics of high yield and small environmental pollution, and has better economic value in preparing the products of the pentafluorobromide benzene.

Description

Technological method for preparing pentafluorobromide benzene
Technical Field
The invention relates to a process method for preparing pentafluorobromide benzene, belonging to the technical field of fine chemical engineering.
Background
Pentafluorobromobenzene is a fine chemical intermediate with wide application, and is mainly used in the fields of medicines and new materials. Six synthetic methods for preparing pentafluorobromide benzene are reported in the literature.
The reaction of pentafluorobenzene with bromine under the catalysis of lewis acid is a classical method for preparing pentafluorobenzene. However, bromine leaks liquid bromine in the transportation and use processes, so that serious personal injury accidents are caused. And bromine is easy to volatilize in the reaction process, so that the utilization rate is not high.
CN102531832 reports that the bromination reaction using potassium bromate and sulfuric acid as bromine sources produces pentafluorobromide benzene in a yield of only 34%.
CN109438168 reports the preparation of pentafluorobromide benzene by bromination reaction under lewis acid catalysis using bromine chloride as a bromine source. The boiling point of bromine chloride is only 10 ℃, and the process operation difficulty is far greater than that of bromine. In addition, the process introduces impurities of the pentafluorobenzene.
CN104529698 reports the reaction of pentafluorophenol with phosphorus tribromide to produce pentafluorobromide benzene. Both pentafluorophenol and phosphorus tribromide are expensive raw materials and this route has no cost advantage.
CN111004089 reports that pentafluorobromine is synthesized in one step by using pentafluorobenzoic acid as a raw material, and the brominating reagent can be bromine, NBS, dibromohydantoin and other brominating reagents. The process has the remarkable advantage of synthesizing the pentafluorobromide benzene from the pentafluorobenzoic acid by one step, and reports that the highest yield is 91%, but 5 times of organic solvent DMF is used, and simultaneously more expensive materials such as pyridine and the like are also used.
Disclosure of Invention
The invention aims to provide a technical method for preparing pentafluorobromide benzene with high yield, which has the remarkable characteristics of high yield and high purity. The dibromohydantoin is adopted to be activated in sulfuric acid to carry out bromination on the pentafluorophenyl to obtain the pentafluorobrominated phenyl. The yield of the crude product of the process reaches more than 97 percent, the yield after rectification reaches 95 percent, and the purity is more than 99 percent. The technical scheme of the process has the remarkable characteristics of high yield and small environmental pollution, and has better economic value in preparing the products of the pentafluorobromide benzene.
The invention discloses a process method for preparing pentafluorobromide benzene, which comprises the following steps:
mixing pentafluorobenzene with concentrated sulfuric acid, controlling the temperature to be 20-40 ℃ and adding an inorganic metal salt activator; adding dibromohydantoin in batches at 20-50 ℃ after the addition; after the addition, controlling the temperature to be 40-80 ℃ to react until the residual content of the pentafluorobenzene is less than 1.0%; after the reaction is finished, cooling and adding the reaction liquid into water, wherein the whole process is not more than 50 ℃; standing for layering, and separating out an organic phase; washing with water to obtain crude product, and rectifying to obtain pentafluorobromide benzene.
Further, in the technical scheme, sulfuric acid is used as a reaction medium in the bromination reaction, and the mixing mass ratio of the pentafluorobenzene to the sulfuric acid is 1:0.5-10; the concentration of sulfuric acid is more than 95%.
Further, in the above technical solution, the activator is selected from zinc sulfate or iron sulfate; the molar ratio of the pentafluorobromide benzene to the activator is 1:0.001-1.
Further, in the above technical scheme, the molar ratio of pentafluorobromobenzene to dibromohydantoin is 1:0.45 to 5.0.
Further, in the technical scheme, after the reaction is finished, the temperature is reduced to 30 ℃, the reaction solution is poured into water, and the temperature of the materials is controlled to be less than 50 ℃.
Further, in the technical scheme, the organic phase is firstly adjusted to be neutral by adopting alkali liquor, and then is washed by water; the yield of the obtained crude product is more than 97%.
Further, in the above technical scheme, the alkaline solution is selected from sodium carbonate, sodium bicarbonate or sodium hydroxide solution; preferably 10% sodium hydroxide solution.
Further, in the technical scheme, the crude product obtained after water washing is purified by a rectifying column to obtain the pentafluorobenzene with the purity of more than 99 percent.
Advantageous effects of the invention
The invention aims to provide a technical method for preparing pentafluorobromide benzene. The yield of the pentafluorobromide benzene prepared by the method can reach more than 95 percent, and the purity can reach more than 99 percent. The technical scheme of the invention has the remarkable characteristics of high yield and small environmental pollution, and has better economic value in preparing the pentafluorobromide benzene product.
DETAILED DESCRIPTION OF EMBODIMENT (S) OF INVENTION
The technical solutions in the embodiments of the present invention will be clearly and completely described below in connection with the embodiments of the present invention. It will be apparent that the described embodiments are only some, but not all, embodiments of the invention. All other embodiments, which can be made by those skilled in the art based on the embodiments of the invention without making any inventive effort, are intended to be within the scope of the invention.
Example 1
100 grams of pentafluorophenyl was mixed with 200 grams of sulfuric acid with stirring, and 1.0 grams of zinc sulfate was added below 40 ℃. 91.9 g of dibromohydantoin are added in batches between 20 and 30 ℃. After dibromohydantoin is added, the reaction is carried out for 10 hours at the temperature of 30-40 ℃. When the starting material remained below 1.0% was regarded as the end point of the reaction. After the reaction, the temperature was lowered to 30 ℃. The reaction solution was poured into water during which the temperature of the material did not exceed 50 ℃. Standing for layering, and separating out an organic phase. The organic phase is washed with water to obtain crude product, and the yield of the crude product is 97%. The crude product is rectified to obtain the pentafluorobromide benzene with 92 percent of yield and 99.7 percent of purity.
Example 2
100 grams of pentafluorophenyl was mixed with 200 grams of sulfuric acid with stirring, and 1.2 grams of ferric sulfate was added below 40 ℃. 91.9 g of dibromohydantoin are added in batches between 20 and 30 ℃. After dibromohydantoin is added, the reaction is carried out for 10 hours at the temperature of 30-40 ℃. When the starting material remained below 1.0% was regarded as the end point of the reaction. After the reaction, the temperature was lowered to 30 ℃. The reaction solution was poured into water during which the temperature of the material did not exceed 50 ℃. Standing for layering, and separating out an organic phase. The organic phase is washed with water to obtain crude product, and the yield of the crude product is 96%. The crude product is rectified to obtain the pentafluorobromide benzene with the yield of 91 percent and the purity of 99.5 percent.
Example 3
100 grams of pentafluorophenyl was mixed with 400 grams of sulfuric acid with stirring, and 1.2 grams of zinc sulfate was added below 40 ℃. 136 g of dibromohydantoin are added in batches between 20 and 30 ℃. After dibromohydantoin is added, the reaction is carried out for 4 hours at the temperature of 30-40 ℃. When the starting material remained below 1.0% was regarded as the end point of the reaction. After the reaction, the temperature was lowered to 30 ℃. The reaction solution was poured into water during which the temperature of the material did not exceed 50 ℃. Standing for layering, and separating out an organic phase. The organic phase is washed with water to obtain crude product, and the yield of the crude product is 98%. The crude product is rectified to obtain the pentafluorobromide benzene with the yield of 93 percent and the purity of 99.3 percent.
Example 4
100 grams of pentafluorophenyl was mixed with 300 grams of sulfuric acid with stirring, and 3.6 grams of zinc sulfate was added below 40 ℃. 91.9 g of dibromohydantoin are added in batches between 20 and 30 ℃. After dibromohydantoin is added, the reaction is carried out for 5 hours at the temperature of 60-80 ℃. When the starting material remained below 1.0% was regarded as the end point of the reaction. After the reaction, the temperature was reduced to 50 ℃. The reaction solution was poured into water during which the temperature of the material did not exceed 50 ℃. Standing for layering, and separating out an organic phase. The organic phase is washed with water to obtain crude product, and the yield of the crude product is 96%. The crude product is rectified to obtain the pentafluorobromide benzene with the yield of 91 percent and the purity of 99.6 percent.
Example 5
100 grams of pentafluorophenyl was mixed with 200 grams of sulfuric acid with stirring, and 0.9 grams of ferrous sulfate was added below 40 ℃. 91.9 g of dibromohydantoin are added in batches between 20 and 30 ℃. After dibromohydantoin is added, the reaction is carried out for 10 hours at the temperature of 30-40 ℃. When the starting material remained below 1.0% was regarded as the end point of the reaction. After the reaction is finished, the temperature is reduced to below 30 ℃. The reaction solution was poured into water during which the temperature of the material did not exceed 50 ℃. Standing for layering, and separating out an organic phase. The organic phase is washed with water to obtain crude product, and the yield of the crude product is 93%. The crude product is rectified to obtain the pentafluorobromide benzene with the yield of 87 percent and the purity of 99.5 percent.
The foregoing embodiments illustrate the basic principles, principal features and advantages of the invention. It will be understood by those skilled in the art that the present invention is not limited to the above-described embodiments, and that the above-described embodiments and descriptions are merely illustrative of the principles of the present invention, and various changes and modifications may be made without departing from the scope of the principles of the invention, which are defined in the appended claims.

Claims (3)

1. The technological method for preparing pentafluorobromide benzene is characterized by comprising the following steps of: 100 g of pentafluorobenzene and 200 g of sulfuric acid are stirred and mixed, and 1.0 g of zinc sulfate is added below 40 ℃; adding 91.9 g of dibromohydantoin in batches at a temperature of between 20 and 30 ℃; after dibromohydantoin is added, controlling the temperature to be 30-40 ℃ for reaction for 10 hours; when the residual content of the raw materials is less than 1.0%, the reaction is regarded as the end point; after the reaction is finished, cooling to 30 ℃; pouring the reaction solution into water, wherein the temperature of the materials is not more than 50 ℃; standing for layering, and separating out an organic phase; washing the organic phase with water to obtain a crude product, wherein the yield of the crude product is 97%; the crude product is rectified to obtain the pentafluorobromide benzene with 92 percent of yield and 99.7 percent of purity.
2. The technological method for preparing pentafluorobromide benzene is characterized by comprising the following steps of: 100 g of pentafluorobenzene and 200 g of sulfuric acid are stirred and mixed, and 1.2 g of ferric sulfate is added below 40 ℃; adding 91.9 g of dibromohydantoin in batches at a temperature of between 20 and 30 ℃; after dibromohydantoin is added, controlling the temperature to be 30-40 ℃ for reaction for 10 hours; when the residual content of the raw materials is less than 1.0%, the reaction is regarded as the end point; after the reaction is finished, cooling to 30 ℃; pouring the reaction solution into water, wherein the temperature of the materials is not more than 50 ℃; standing for layering, and separating out an organic phase; washing the organic phase with water to obtain a crude product, wherein the yield of the crude product is 96%; the crude product is rectified to obtain the pentafluorobromide benzene with the yield of 91 percent and the purity of 99.5 percent.
3. The technological method for preparing pentafluorobromide benzene is characterized by comprising the following steps of: 100 g of pentafluorobenzene and 300 g of sulfuric acid are stirred and mixed, and 3.6 g of zinc sulfate is added below 40 ℃; adding 91.9 g of dibromohydantoin in batches at a temperature of between 20 and 30 ℃; after dibromohydantoin is added, controlling the temperature to be 60-80 ℃ for reaction for 5 hours; when the residual content of the raw materials is less than 1.0%, the reaction is regarded as the end point; after the reaction is finished, cooling to 50 ℃; pouring the reaction solution into water, wherein the temperature of the materials is not more than 50 ℃; standing for layering, and separating out an organic phase; washing the organic phase with water to obtain a crude product, wherein the yield of the crude product is 96%; the crude product is rectified to obtain the pentafluorobromide benzene with the yield of 91 percent and the purity of 99.6 percent.
CN202210154859.2A 2022-02-19 2022-02-19 Technological method for preparing pentafluorobromide benzene Active CN114920622B (en)

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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0665120A (en) * 1992-08-12 1994-03-08 Seimi Chem Co Ltd Production of bromopentafluorobenzene
CN101759597A (en) * 2009-12-31 2010-06-30 上海康鹏化学有限公司 Preparation method of 2-trifluoromethyl-4-aminobenzonitrile
CN109438168A (en) * 2018-11-13 2019-03-08 大连奇凯医药科技有限公司 The preparation method of five bromofluorobenzenes

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0665120A (en) * 1992-08-12 1994-03-08 Seimi Chem Co Ltd Production of bromopentafluorobenzene
CN101759597A (en) * 2009-12-31 2010-06-30 上海康鹏化学有限公司 Preparation method of 2-trifluoromethyl-4-aminobenzonitrile
CN109438168A (en) * 2018-11-13 2019-03-08 大连奇凯医药科技有限公司 The preparation method of five bromofluorobenzenes

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