WO2019084977A1 - Production method for vinylidene fluoride monomer - Google Patents
Production method for vinylidene fluoride monomer Download PDFInfo
- Publication number
- WO2019084977A1 WO2019084977A1 PCT/CN2017/109708 CN2017109708W WO2019084977A1 WO 2019084977 A1 WO2019084977 A1 WO 2019084977A1 CN 2017109708 W CN2017109708 W CN 2017109708W WO 2019084977 A1 WO2019084977 A1 WO 2019084977A1
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- WO
- WIPO (PCT)
- Prior art keywords
- vinylidene fluoride
- introducing
- passing
- fluoride monomer
- chloroethane
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C17/00—Preparation of halogenated hydrocarbons
- C07C17/25—Preparation of halogenated hydrocarbons by splitting-off hydrogen halides from halogenated hydrocarbons
Definitions
- the present invention relates to a process for producing a vinylidene fluoride monomer.
- the method for producing VDF monomer mainly uses difluorochloroethane as a raw material, and is subjected to air tube cracking or water vapor dilution cracking, and after a series of pretreatment steps, the VDF monomer is finally obtained by rectification.
- the cracking is insufficient, resulting in excessive waste of raw materials.
- the object of the present invention is to solve the above problems.
- the technical solution of the present invention is to design a method for producing a vinylidene fluoride monomer, comprising the following steps:
- the vinylidene fluoride is passed through a rectification column to a vinylidene fluoride monomer.
- the invention has the advantages and beneficial effects of providing a method for producing a vinylidene fluoride monomer, which is divided into a primary cracking process and a secondary cracking process, and a lower primary cracking temperature mainly serves as a preheating effect on the raw material gas. And partial cracking, the secondary cracking temperature is higher, and the raw material gas is further cracked.
- the production method of the vinylidene fluoride monomer of the invention can effectively improve the production efficiency and reduce the waste of raw materials.
- a method for producing a vinylidene fluoride monomer comprising the steps of:
- the vinylidene fluoride is passed through a rectification column to a vinylidene fluoride monomer.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
本发明涉及一种偏氟乙烯单体的生产方法。The present invention relates to a process for producing a vinylidene fluoride monomer.
目前生产VDF单体的方法主要采用二氟一氯乙烷作为原料,通过空管裂解或者水蒸气稀释裂解,在经过一系列的前处理步骤,最终通过精馏得到VDF单体。该方法在实际生产过程中,裂解不充分,导致原料浪费过大。At present, the method for producing VDF monomer mainly uses difluorochloroethane as a raw material, and is subjected to air tube cracking or water vapor dilution cracking, and after a series of pretreatment steps, the VDF monomer is finally obtained by rectification. In the actual production process, the cracking is insufficient, resulting in excessive waste of raw materials.
发明内容Summary of the invention
本发明的目的在于旨在解决上述问题。The object of the present invention is to solve the above problems.
为了实现上述目的,本发明的技术方案是设计一种偏氟乙烯单体的生产方法,包括如下步骤:In order to achieve the above object, the technical solution of the present invention is to design a method for producing a vinylidene fluoride monomer, comprising the following steps:
1)采用二氟一氯乙烷作为原料,通入一级裂解炉,裂解温度450℃,反应1h;1) using difluoro-chloroethane as a raw material, passing into a primary cracking furnace, the cracking temperature is 450 ° C, and reacting for 1 h;
2)将上述裂解气通入二级裂解炉,裂解温度1100℃;2) The above cracked gas is passed into the secondary cracking furnace, and the cracking temperature is 1100 ° C;
3)将上述气体通过依次反应缓冲装置、压缩机、冷凝器,并采用回收装置回收未参与反应的二氟一氯乙烷,回收的二氟一氯乙烷重新进入一级裂解炉;3) passing the above gas through a sequential reaction buffer device, a compressor, a condenser, and recovering the difluorochloroethane which is not involved in the reaction by using a recovery device, and the recovered difluorochloroethane is re-entered into the primary cracking furnace;
4)将经过冷凝器的偏氟乙烯通入脱轻塔脱除轻组分;4) passing the vinylidene fluoride passing through the condenser into the de-lighting tower to remove the light component;
5)偏氟乙烯经过精馏塔等到偏氟乙烯单体。5) The vinylidene fluoride is passed through a rectification column to a vinylidene fluoride monomer.
本发明的优点和有益效果在于:提供一种偏氟乙烯单体的生产方法,将裂解过程分为一级裂解和二级裂解,一级裂解温度较低主要起到对原料气体的预热作用并部分裂解,二级裂解温度较高,对原料气体进一步裂解。采用本发明的一种偏氟乙烯单体的生产方法能有效提高生产效率,降低原料浪费。The invention has the advantages and beneficial effects of providing a method for producing a vinylidene fluoride monomer, which is divided into a primary cracking process and a secondary cracking process, and a lower primary cracking temperature mainly serves as a preheating effect on the raw material gas. And partial cracking, the secondary cracking temperature is higher, and the raw material gas is further cracked. The production method of the vinylidene fluoride monomer of the invention can effectively improve the production efficiency and reduce the waste of raw materials.
下面结合附图和实施例,对本发明的具体实施方式作进一步描述。以下实施例仅用于更加清楚地说明本发明的技术方案,而不能以此来限制本发明的保护范围。The specific embodiments of the present invention are further described below in conjunction with the drawings and embodiments. The following examples are only intended to more clearly illustrate the technical solutions of the present invention, and are not intended to limit the scope of the present invention.
实施例:Example:
一种偏氟乙烯单体的生产方法,包括如下步骤:A method for producing a vinylidene fluoride monomer, comprising the steps of:
1)采用二氟一氯乙烷作为原料,通入一级裂解炉,裂解温度450℃,反应1h;1) using difluoro-chloroethane as a raw material, passing into a primary cracking furnace, the cracking temperature is 450 ° C, and reacting for 1 h;
2)将上述裂解气通入二级裂解炉,裂解温度1100℃;2) The above cracked gas is passed into the secondary cracking furnace, and the cracking temperature is 1100 ° C;
3)将上述气体通过依次反应缓冲装置、压缩机、冷凝器,并采用回收装置回收未参与反应 的二氟一氯乙烷,回收的二氟一氯乙烷重新进入一级裂解炉;3) passing the above gas through a sequential reaction buffer device, a compressor, a condenser, and recovering the non-reactive reaction by using a recovery device. Difluorochloroethane, recovered difluorochloroethane re-entered into the primary cracking furnace;
4)将经过冷凝器的偏氟乙烯通入脱轻塔脱除轻组分;4) passing the vinylidene fluoride passing through the condenser into the de-lighting tower to remove the light component;
5)偏氟乙烯经过精馏塔等到偏氟乙烯单体。5) The vinylidene fluoride is passed through a rectification column to a vinylidene fluoride monomer.
以上所述仅是本发明的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明技术原理的前提下,还可以做出若干改进和润饰,这些改进和润饰也应视为本发明的保护范围。 The above description is only a preferred embodiment of the present invention, and it should be noted that those skilled in the art can make several improvements and retouchings without departing from the technical principles of the present invention. It should also be considered as the scope of protection of the present invention.
Claims (1)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711076337.0A CN107721813A (en) | 2017-11-06 | 2017-11-06 | Production method of vinylidene fluoride monomer |
| CN201711076337.0 | 2017-11-06 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2019084977A1 true WO2019084977A1 (en) | 2019-05-09 |
Family
ID=61222420
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/CN2017/109708 Ceased WO2019084977A1 (en) | 2017-11-06 | 2017-11-07 | Production method for vinylidene fluoride monomer |
Country Status (2)
| Country | Link |
|---|---|
| CN (1) | CN107721813A (en) |
| WO (1) | WO2019084977A1 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110776394B (en) * | 2019-11-07 | 2022-06-10 | 上海华谊三爱富新材料有限公司 | Method for preparing fluorine-containing ethylene by catalytic cracking of 2-chloro-1, 1-difluoroethane |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4053529A (en) * | 1975-07-18 | 1977-10-11 | Solvay & Cie | Process for the manufacture of vinylidene fluoride |
| CN103664509A (en) * | 2013-12-18 | 2014-03-26 | 常熟振氟新材料有限公司 | Production system of vinylidene fluoride |
| CN104557446A (en) * | 2014-12-15 | 2015-04-29 | 东莞市长安东阳光铝业研发有限公司 | Method for preparing vinylidene fluoride monomer |
| KR101571532B1 (en) * | 2014-08-11 | 2015-11-24 | 한국화학연구원 | The preparing apparatus of vinylidene fluorid |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4178316A (en) * | 1976-12-31 | 1979-12-11 | Dynamit Nobel Aktiengesellschaft | Method of preparing 1,1-difluoroethylene from acetylene |
| CN1223560C (en) * | 2001-12-25 | 2005-10-19 | 中昊晨光化工研究院 | Method for producing metafluoroethylene by pyrolysis of difluoro-chloroethane |
-
2017
- 2017-11-06 CN CN201711076337.0A patent/CN107721813A/en active Pending
- 2017-11-07 WO PCT/CN2017/109708 patent/WO2019084977A1/en not_active Ceased
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4053529A (en) * | 1975-07-18 | 1977-10-11 | Solvay & Cie | Process for the manufacture of vinylidene fluoride |
| CN103664509A (en) * | 2013-12-18 | 2014-03-26 | 常熟振氟新材料有限公司 | Production system of vinylidene fluoride |
| KR101571532B1 (en) * | 2014-08-11 | 2015-11-24 | 한국화학연구원 | The preparing apparatus of vinylidene fluorid |
| CN104557446A (en) * | 2014-12-15 | 2015-04-29 | 东莞市长安东阳光铝业研发有限公司 | Method for preparing vinylidene fluoride monomer |
Also Published As
| Publication number | Publication date |
|---|---|
| CN107721813A (en) | 2018-02-23 |
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