WO2010054540A1 - A method for preparing chloromethyl-1,1,1,3,3,3- hexafluoroisopropyl ether - Google Patents

A method for preparing chloromethyl-1,1,1,3,3,3- hexafluoroisopropyl ether Download PDF

Info

Publication number
WO2010054540A1
WO2010054540A1 PCT/CN2009/070530 CN2009070530W WO2010054540A1 WO 2010054540 A1 WO2010054540 A1 WO 2010054540A1 CN 2009070530 W CN2009070530 W CN 2009070530W WO 2010054540 A1 WO2010054540 A1 WO 2010054540A1
Authority
WO
WIPO (PCT)
Prior art keywords
reaction
chloride
hexafluoro
lewis acid
propanol
Prior art date
Application number
PCT/CN2009/070530
Other languages
French (fr)
Chinese (zh)
Inventor
孙飘扬
童达君
李迎宾
卢长娟
刘潇
梅杰
Original Assignee
江苏恒瑞医药股份有限公司
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by 江苏恒瑞医药股份有限公司 filed Critical 江苏恒瑞医药股份有限公司
Publication of WO2010054540A1 publication Critical patent/WO2010054540A1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C41/00Preparation of ethers; Preparation of compounds having groups, groups or groups
    • C07C41/01Preparation of ethers

Definitions

  • the present invention relates to a process for the preparation of hexafluoroisopropyl ether, in particular to a process for the preparation of chloromethyl-1,1,3,3,3-hexafluoroisopropyl ether, from 1,1, 1,3, Binary catalytic system of 3,3-hexafluoro-2-propanol and 1,3,5-trioxanthene or paraformaldehyde in the main catalyst with anhydrous chlorinated Lewis acid and chlorine-containing compound as cocatalyst The reaction takes place to form chloromethyl-1,1,1,3,3,3-hexafluoroisopropyl ether.
  • Chloromethyl-1,1,1,3,3,3-hexafluoroisopropyl ether is an important intermediate for the synthesis of fluoromethyl-1,1,1,3,3,3-hexafluoroisopropyl ether .
  • the latter formula (CF 3 ) 2 CHOCH 2 F referred to as sevoflurane.
  • sevoflurane has the characteristics of induction of anesthesia and rapid recovery, but also reduces cerebral vascular resistance, brain metabolic rate, brain oxygen consumption, myocardial contractile function and blood pressure, and is significantly less irritating to the respiratory tract.
  • Other inhaled anesthetics have not seen liver and kidney toxicity. This is precisely the most desirable nature of modern inhalation anesthetics.
  • sevoflurane has received extensive attention and attention internationally.
  • U.S. Patent No. US4,250,334 and US4,469,898 describes the production of sevoflurane technical route, have taught with 1,1,1,3,3,3-hexafluoro-2-propanol (formula (CF 3) 2 CHOH , hereinafter referred to as HFIP) as a raw material for the reaction.
  • HFIP 1,1,1,3,3,3-hexafluoro-2-propanol
  • U.S. Patent No. 4,469,8,98 the disclosure of HFIP to form sevoflurane with formaldehyde and hydrogen fluoride, protonating reagents, dehydrating reagents and fluorinating reagents;
  • U.S. Patent 4,250,334 describes another technical route for the addition of HFIP to excess polymerization.
  • the reaction is carried out in formaldehyde and hydrogen fluoride, while excess sulfuric acid is used to absorb the water generated during the reaction.
  • the synthesis methods described in these two U.S. patents require the purification of the product due to the presence of by-products, and these by-products are difficult to remove; the use of highly corrosive hydrogen fluoride reagents and sulfuric acid in the production requires corrosion protection of the equipment. High, to some extent, increase the production cost of sevoflurane.
  • U.S. Patent No. 6,469,219 teaches direct fluorination of methyl hexafluoroisopropyl ether. Direct reaction requires the use of an extremely active BrF 3 reagent to fluorinate methyl hexafluoroisopropyl ether. In this anti 0.5-lmol of BrF 3 is required to react with 0.67 mol of methyl hexafluoroisopropyl ether, and the reaction temperature is controlled between 20 and 50 °C. Direct fluorination can also be carried out directly with fluorine gas under argon protection.
  • U.S. Patent No. 5,705,710 teaches the synthesis of sevoflurane using methoxymalononitrile and a highly active oxidizing fluorinating agent, bromine trifluoride.
  • the intermediate chloromethyl-1,1,1,3,3,3-hexafluoroisopropyl ether and the by-product H0A1C1 2 are formed , followed by the addition of 6N HCl to remove the by-product H0A1C1 2 , and finally the intermediate chloromethyl group - 1,1,1,3,3,3-hexafluoroisopropyl ether is reacted with a fluorinating reagent or a solvent to obtain sevoflurane.
  • a fluorinating reagent or a solvent to obtain sevoflurane.
  • the molar ratio of the chlorinated Lewis acid to the chlorine-containing compound is from 1:0.01 to 1:5.
  • the molar ratio of the Lewis acid to the chlorine-containing compound should be controlled from 1:0.01 to 1:2.
  • the molar ratio of 1,1,1,3,3,3-hexafluoro-2-propanol to the Lewis acid chloride is 1:0.1 to 1:5, and the optimum molar ratio is 1:0.1 to 1:2.
  • the chlorinated Lewis acid is selected from the group consisting of phosphorus trichloride, aluminum trichloride, ferric chloride or tin tetrachloride.
  • the chlorine-containing compound is selected from the group consisting of sodium chloride, potassium chloride, lithium chloride, thionyl chloride, sulfuryl chloride or aluminum trichloride.
  • reaction time is controlled to 5 to 8 hours.
  • the invention has the advantages of greatly improving the original process by using a low-cost binary catalytic system, greatly shortening the reaction time, and greatly improving the chloromethyl-1,1,1,3,3,3-hexafluoroiso The yield of propyl ether.
  • the purity of chloromethyl-1,1,1,3,3,3-hexafluoroisopropyl ether was 98% or more, and the yield was 87% or more.
  • the reaction of the binary catalyst technical scheme is an exothermic reaction.
  • 1,3,5-trioxinium is used, the reaction proceeds slowly, and the process can be controlled relatively smoothly.
  • paraformaldehyde the reaction proceeds relatively quickly, but the exotherm is compared. severe. In theory, both can be used, but it depends on the specific situation and requirements.
  • a chlorinated Lewis acid is used to activate 1,3,5-trioxolane or paraformaldehyde and is used as a chlorinated group.
  • the molar ratio of HFIP (purity 99%) to 1,3,5-trioxin or paraformaldehyde added in the reaction is 1:0.5 to 1:5; the molar ratio of HFIP to Lewis acid is 1 : 0.1 to 1:5.
  • the chlorinated Lewis acid is one of phosphorus trichloride, aluminum trichloride, ferric chloride and tin tetrachloride.
  • the reaction can be controlled at a temperature of from -20 ° C to 50 ° C.
  • the chlorine-containing compound is one of sodium chloride, potassium chloride, lithium chloride, thionyl chloride, sulfuryl chloride, and aluminum trichloride.
  • the molar ratio of the chlorinated Lewis acid to the chlorine-containing compound is from 1:0.01 to 1:5. In order to allow the reaction to proceed better, the molar ratio of the chlorinated Lewis acid to the chlorine-containing compound should be controlled from 1:0.01 to 1:2.
  • the by-product H0A1C1 2 produced in the reaction has certain toxicity to chloromethyl-1,1,1,3,3,3-hexafluoroisopropyl ether, which leads to chloromethyl-1,1,1,3. Degradation of 3,3-hexafluoroisopropyl ether.
  • chloride ions in the product act as a Lewis acid, causing degradation of chloromethyl-1,1,1,3,3,3-hexafluoroisopropyl ether.
  • the method of removal is also simple.
  • the prior art method can be used, for example, by diluting hydrochloric acid to decompose it, and the recovered H0A1C1 2 can be further reacted to prepare a raw material for the reaction, which is a chlorinated Lewis acid.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Disclosed is a method for preparing chloromethyl-1,1,1,3,3,3-hexafluoroisopropyl ether, which is combining hexafluoroisopropanol and either 1,3,5-trixane or paraformaldehyde in the presence of  a binary catalyst system to produce chloromethyl-1,1,1,3,3,3-hexafluoroisopropyl ether, where in the binary catalyst system is consisted of an anhydrous chlorinating Lewis acid as the main catalyst and a chlorine-containing compound as the cocatalyst.

Description

制备氯甲基 -1,U,3,3,3-六氟异丙基醚的方法 技术领域  Process for the preparation of chloromethyl-1,U,3,3,3-hexafluoroisopropyl ether
本发明涉及制备六氟异丙基醚的方法, 特别是制备氯甲基 -1,1, 1,3,3,3-六氟异丙基醚的方法, 由 1,1, 1,3,3,3-六氟 -2-丙醇和 1,3,5-三 氧杂环己垸或低聚甲醛在以无水氯化路易斯酸为主催化剂, 含氯化合 物为助催化剂的二元催化体系中发生反应生成氯甲基 -1,1,1,3,3,3-六氟 异丙基醚。 技术背景  The present invention relates to a process for the preparation of hexafluoroisopropyl ether, in particular to a process for the preparation of chloromethyl-1,1,3,3,3-hexafluoroisopropyl ether, from 1,1, 1,3, Binary catalytic system of 3,3-hexafluoro-2-propanol and 1,3,5-trioxanthene or paraformaldehyde in the main catalyst with anhydrous chlorinated Lewis acid and chlorine-containing compound as cocatalyst The reaction takes place to form chloromethyl-1,1,1,3,3,3-hexafluoroisopropyl ether. technical background
氯甲基 -1,1,1,3,3,3-六氟异丙基醚是合成氟甲基 -1,1,1,3,3,3-六氟异 丙基醚的重要中间体。 后者分子式 (CF3)2CHOCH2F, 简称七氟醚。 在 最近几年里, 研究发现七氟醚具有诱导麻醉和苏醒快速的特性, 还可 降低脑血管阻力、 脑代谢率、 脑耗氧量、 心肌收缩功能和血压, 对呼 吸道的刺激性明显低于其他吸入麻醉剂, 尚未见其肝肾毒性。 而这恰 恰又是现代吸入麻醉剂最需要的性质, 七氟醚作为一种新型的吸入式 麻醉剂, 在国际上受到广泛的关注和重视。 Chloromethyl-1,1,1,3,3,3-hexafluoroisopropyl ether is an important intermediate for the synthesis of fluoromethyl-1,1,1,3,3,3-hexafluoroisopropyl ether . The latter formula (CF 3 ) 2 CHOCH 2 F, referred to as sevoflurane. In recent years, studies have found that sevoflurane has the characteristics of induction of anesthesia and rapid recovery, but also reduces cerebral vascular resistance, brain metabolic rate, brain oxygen consumption, myocardial contractile function and blood pressure, and is significantly less irritating to the respiratory tract. Other inhaled anesthetics have not seen liver and kidney toxicity. This is precisely the most desirable nature of modern inhalation anesthetics. As a new type of inhaled anesthetic, sevoflurane has received extensive attention and attention internationally.
美国专利 US4,250,334 和 US4,469,898 描述了生产七氟醚的技术 路线, 都教导用 1,1,1,3,3,3-六氟 -2-丙醇 (分子式为 (CF3) 2CHOH , 以下简称 HFIP)作为反应原料。美国专利 US4,469,898 中, 由 HFIP 同 甲醛和氟化氢、 质子化试剂、 脱水试剂和氟化试剂反应生成七氟醚; 美国专利 US4,250,334 描述了另外一条技术路线, 把 HFIP加入到过 量的多聚甲醛和氟化氢中进行反应, 同时用过量的硫酸来吸收反应过 程中产生的水分。 这二篇美国专利所描述合成方法, 由于副产物的存 在都需要对产物进行纯化, 而且这些副产物很难被除去; 生产中使用 腐蚀性极强的氟化氢试剂和硫酸对设备的防腐蚀要求较高, 在一定程 度上提高了七氟醚的生产成本。 U.S. Patent No. US4,250,334 and US4,469,898 describes the production of sevoflurane technical route, have taught with 1,1,1,3,3,3-hexafluoro-2-propanol (formula (CF 3) 2 CHOH , hereinafter referred to as HFIP) as a raw material for the reaction. U.S. Patent No. 4,469,8,98, the disclosure of HFIP to form sevoflurane with formaldehyde and hydrogen fluoride, protonating reagents, dehydrating reagents and fluorinating reagents; U.S. Patent 4,250,334 describes another technical route for the addition of HFIP to excess polymerization. The reaction is carried out in formaldehyde and hydrogen fluoride, while excess sulfuric acid is used to absorb the water generated during the reaction. The synthesis methods described in these two U.S. patents require the purification of the product due to the presence of by-products, and these by-products are difficult to remove; the use of highly corrosive hydrogen fluoride reagents and sulfuric acid in the production requires corrosion protection of the equipment. High, to some extent, increase the production cost of sevoflurane.
美国专利 US6,469,219 教导直接氟化甲基六氟异丙基醚。 直接反 应需要使用极其活泼的 BrF3试剂来氟化甲基六氟异丙基醚。在这个反 应中需要 0.5-lmol 的 BrF3 来和 0.67mol的甲基六氟异丙基醚反应,反 应温度控制在 20-50°C之间。直接氟化还可以在氩气保护下用氟气来直 接进行氟化。 美国专利 US5,705,710 教导用甲氧基丙二腈和强活性氧 化氟化剂三氟化溴来合成七氟醚。 U.S. Patent No. 6,469,219 teaches direct fluorination of methyl hexafluoroisopropyl ether. Direct reaction requires the use of an extremely active BrF 3 reagent to fluorinate methyl hexafluoroisopropyl ether. In this anti 0.5-lmol of BrF 3 is required to react with 0.67 mol of methyl hexafluoroisopropyl ether, and the reaction temperature is controlled between 20 and 50 °C. Direct fluorination can also be carried out directly with fluorine gas under argon protection. U.S. Patent No. 5,705,710 teaches the synthesis of sevoflurane using methoxymalononitrile and a highly active oxidizing fluorinating agent, bromine trifluoride.
在众多的研究七氟醚的专利中, 美国雅培公司的专利 US6,100,434、 US6,245,949B1、 US6,271,422和 US6,303,831所描述的 生产七氟醚的技术路最为可行。其中又以 US6,100,434中所描述的方法 最为经济实用。 该法用 1,1,1,3,3,3-六氟 -2-丙醇、 1,3,5-三氧杂环己垸或 低聚甲醛和无水氯化铝反应 20小时后, 生成中间体氯甲基 -1,1,1,3,3,3- 六氟异丙基醚和副产物 H0A1C12, 接着加入 6N HC1分解去除副产物 H0A1C12 , 最后由中间体氯甲基 -1,1,1,3,3,3-六氟异丙基醚与氟化试剂、 溶剂反应来制取七氟醚。 它的优点在于原料价格低廉不带腐蚀性, 对 设备要求不高, 操作简便。 但是该法中的反应中间体氯甲基 -1,1,1,3,3,3- 六氟异丙基醚收率比较低, 纯度不高。 Among the numerous patents for the study of sevoflurane, the technical routes for the production of sevoflurane described in U.S. Patent Nos. 6,100,434, 6,245,949 B1, US 6,271,422 and US 6,303,831 are most feasible. Among them, the method described in US 6,100,434 is the most economical and practical. The method is reacted with 1,1,1,3,3,3-hexafluoro-2-propanol, 1,3,5-trioxanthene or paraformaldehyde and anhydrous aluminum chloride for 20 hours. The intermediate chloromethyl-1,1,1,3,3,3-hexafluoroisopropyl ether and the by-product H0A1C1 2 are formed , followed by the addition of 6N HCl to remove the by-product H0A1C1 2 , and finally the intermediate chloromethyl group - 1,1,1,3,3,3-hexafluoroisopropyl ether is reacted with a fluorinating reagent or a solvent to obtain sevoflurane. Its advantage is that the raw materials are inexpensive and non-corrosive, and the equipment requirements are not high and the operation is simple. However, the reaction intermediate of the method, chloromethyl-1,1,1,3,3,3-hexafluoroisopropyl ether, has a relatively low yield and a low purity.
最近的国际专利申请, 公开号 WO2008/037039教导通过加浓硫酸 或发烟硫酸来得到高纯度和高收率的氯甲基 -1,1,1,3,3,3-六氟异丙基醚, 但是浓硫酸或发烟硫酸对设备有很强烈的腐蚀性。 发明内容  The recent international patent application, Publication No. WO 2008/037039 teaches obtaining high purity and high yield of chloromethyl-1,1,1,3,3,3-hexafluoroisopropyl by enriching sulfuric acid or fuming sulfuric acid. Ether, but concentrated sulfuric acid or fuming sulfuric acid is very corrosive to equipment. Summary of the invention
为了克服现有技术的不足之处, 本发明的目的在于提供一种氯甲 基 -1,1,1,3,3,3-六氟异丙基醚的制备方法。 该方法终产物产量高 (至少 87%), 纯度高(至少 98% ), 反应过程简单、 经济适用、 无腐蚀性、 符 合环保要求。  In order to overcome the deficiencies of the prior art, it is an object of the present invention to provide a process for the preparation of chloromethyl-1,1,1,3,3,3-hexafluoroisopropyl ether. The method has high yield (at least 87%) and high purity (at least 98%). The reaction process is simple, economical, non-corrosive and environmentally friendly.
为实现上述目的, 本发明采用的技术方案是:  In order to achieve the above object, the technical solution adopted by the present invention is:
采用 1,1,1,3,3,3-六氟 -2-丙醇和 1,3,5-三氧杂环己垸或低聚甲醛在以 无水氯化路易斯酸为主催化剂, 含氯化合物为助催化剂的二元催化体 系中发生反应生成氯甲基 -1,1,1,3,3,3-六氟异丙基醚。  Using 1,1,1,3,3,3-hexafluoro-2-propanol and 1,3,5-trioxanthene or paraformaldehyde in the main catalyst of anhydrous Lewis acid, chlorine The reaction occurs in a binary catalytic system in which the compound is a cocatalyst to form chloromethyl-1,1,1,3,3,3-hexafluoroisopropyl ether.
其中, 氯化路易斯酸和含氯化合物的摩尔比为 1:0.01至 1:5。 为了 使反应更好地进行, 氯化路易斯酸和含氯化合物的摩尔比为应控制在 1:0.01至 1:2。  Wherein, the molar ratio of the chlorinated Lewis acid to the chlorine-containing compound is from 1:0.01 to 1:5. In order to allow the reaction to proceed better, the molar ratio of the Lewis acid to the chlorine-containing compound should be controlled from 1:0.01 to 1:2.
1,1,1,3,3,3-六氟 -2-丙醇与 1,3,5-三氧杂环己垸或低聚甲醛的摩尔比 为 1: 0.5 至 1:5, 最优摩尔比为 1: 0.5 至 1:2。 Molar ratio of 1,1,1,3,3,3-hexafluoro-2-propanol to 1,3,5-trioxanthene or paraformaldehyde The ratio is 1:0.5 to 1:5, and the optimum molar ratio is 1:0.5 to 1:2.
1,1,1,3,3,3-六氟 -2-丙醇与氯化路易斯酸的摩尔比为 1: 0.1 至 1:5, 最优摩尔比为 1 : 0.1 至 1:2。  The molar ratio of 1,1,1,3,3,3-hexafluoro-2-propanol to the Lewis acid chloride is 1:0.1 to 1:5, and the optimum molar ratio is 1:0.1 to 1:2.
所述的氯化路易斯酸选自三氯化磷、 三氯化铝、 三氯化铁或者四 氯化锡。  The chlorinated Lewis acid is selected from the group consisting of phosphorus trichloride, aluminum trichloride, ferric chloride or tin tetrachloride.
所述的含氯化合物选自氯化钠、 氯化钾、 氯化锂、 二氯亚砜、 硫 酰氯或者三氯化铝。  The chlorine-containing compound is selected from the group consisting of sodium chloride, potassium chloride, lithium chloride, thionyl chloride, sulfuryl chloride or aluminum trichloride.
其中, 反应时间控制在 5至 8小时。  Among them, the reaction time is controlled to 5 to 8 hours.
本发明的优点在于利用价格低廉的二元催化体系, 大幅度改善原 有工艺, 大幅缩短了反应时间, 且极大地提高氯甲基 -1,1,1,3,3,3-六氟 异丙基醚收率。氯甲基 -1,1,1,3,3,3-六氟异丙基醚的纯度达到 98%以上, 收率达到 87%以上。 具体实施方式
Figure imgf000004_0001
The invention has the advantages of greatly improving the original process by using a low-cost binary catalytic system, greatly shortening the reaction time, and greatly improving the chloromethyl-1,1,1,3,3,3-hexafluoroiso The yield of propyl ether. The purity of chloromethyl-1,1,1,3,3,3-hexafluoroisopropyl ether was 98% or more, and the yield was 87% or more. Detailed ways
Figure imgf000004_0001
CF3CHCF3 CF.qCHCF CF 3 CHCF 3 CF.qCHCF
二元催化剂 技术方案的反应为放热反应。 当使用 1,3,5-三氧杂环己垸时, 反应 进行得比较缓慢, 过程可以得到比较平稳的控制; 而当使用低聚甲醛 时, 反应进行得比较迅速、 但放热现象来得比较剧烈。 理论上两者都 可以使用, 但需按照具体情况和要求而定。 而在反应中加入氯化路易 斯酸是用来激活 1,3,5-三氧杂环己垸或低聚甲醛, 并作为一种氯化基团 来使用的。 在反应中加入的 HFIP (纯度 99 % ) 与 1,3,5-三氧杂环己 垸或者低聚甲醛摩尔比为 1:0.5至 1:5; HFIP与氯化路易斯酸的摩尔比 为 1:0.1至 1:5。 其中氯化路易斯酸是三氯化磷、 三氯化铝、 三氯化铁、 四氯化锡中的一种。 该反应可以控制在 -20 °C-50°C温度条件下进行。 含氯化合物为氯化钠、 氯化钾、 氯化锂、 二氯亚砜、 硫酰氯、 三氯化 铝中的一种。 氯化路易斯酸和含氯化合物的摩尔比为 1:0.01至 1:5。 为 了使反应更好地进行, 氯化路易斯酸和含氯化合物的摩尔比为应控制 在 1:0.01至 1:2。 反应中生成的副产物 H0A1C12对氯甲基 -1,1,1,3,3,3-六氟异丙基醚 具有一定的毒性, 会导致氯甲基 -1,1,1,3,3,3-六氟异丙基醚的降解。 特 别是产物中的氯离子会作为一种路易斯酸, 而造成氯甲基 -1,1,1,3,3,3- 六氟异丙基醚的降解。 所以, 最好除去产生的 H0A1C12 。 除去的方法 也很简单, 采用现有技术的方法, 例如可以加入稀盐酸使其分解, 回 收后的 H0A1C12又可以通过进一步的反应来制备反应所需的原料氯化 路易斯酸。 实施例 1 The reaction of the binary catalyst technical scheme is an exothermic reaction. When 1,3,5-trioxinium is used, the reaction proceeds slowly, and the process can be controlled relatively smoothly. When using paraformaldehyde, the reaction proceeds relatively quickly, but the exotherm is compared. severe. In theory, both can be used, but it depends on the specific situation and requirements. The addition of a chlorinated Lewis acid to the reaction is used to activate 1,3,5-trioxolane or paraformaldehyde and is used as a chlorinated group. The molar ratio of HFIP (purity 99%) to 1,3,5-trioxin or paraformaldehyde added in the reaction is 1:0.5 to 1:5; the molar ratio of HFIP to Lewis acid is 1 : 0.1 to 1:5. The chlorinated Lewis acid is one of phosphorus trichloride, aluminum trichloride, ferric chloride and tin tetrachloride. The reaction can be controlled at a temperature of from -20 ° C to 50 ° C. The chlorine-containing compound is one of sodium chloride, potassium chloride, lithium chloride, thionyl chloride, sulfuryl chloride, and aluminum trichloride. The molar ratio of the chlorinated Lewis acid to the chlorine-containing compound is from 1:0.01 to 1:5. In order to allow the reaction to proceed better, the molar ratio of the chlorinated Lewis acid to the chlorine-containing compound should be controlled from 1:0.01 to 1:2. The by-product H0A1C1 2 produced in the reaction has certain toxicity to chloromethyl-1,1,1,3,3,3-hexafluoroisopropyl ether, which leads to chloromethyl-1,1,1,3. Degradation of 3,3-hexafluoroisopropyl ether. In particular, chloride ions in the product act as a Lewis acid, causing degradation of chloromethyl-1,1,1,3,3,3-hexafluoroisopropyl ether. Therefore, it is preferable to remove the generated H0A1C1 2 . The method of removal is also simple. The prior art method can be used, for example, by diluting hydrochloric acid to decompose it, and the recovered H0A1C1 2 can be further reacted to prepare a raw material for the reaction, which is a chlorinated Lewis acid. Example 1
250ml 干燥三口瓶中加入 27.0g ( 0.20mol ) 无水 A1C13和 8.5gAdd 27.0g (0.20mol) of anhydrous A1C1 3 and 8.5g to a 250ml dry three-necked vial
(0.20mol ) LiCl, 搅拌冷至 -5°C, 滴加 20.5ml (0.20mol ) 1,1,1,3,3,3- 六氟 -2-丙醇 (滴加时间 10分钟)。 滴完后, 续搅 15分钟, 加入 9.0g (0.30mol) 低聚甲醛, 移掉冷浴, 室温搅拌白色混合物 8小时。 反应 完后, 降温至 -5 °C, 滴加 100ml 5N盐酸和 20ml水, 搅拌 1小时后静 置。 分离有机相 (下层), 得 37.9g无色液体, 收率为 88.1 %。 气相色 谱分析其纯度为 99.3 %。 (0.20 mol) LiCl, cooled to -5 °C, and 20.5 ml (0.20 mol) of 1,1,1,3,3,3-hexafluoro-2-propanol (drip time 10 minutes) was added dropwise. After the completion of the dropwise addition, the mixture was continuously stirred for 15 minutes, 9.0 g (0.30 mol) of paraformaldehyde was added, the cooling bath was removed, and the white mixture was stirred at room temperature for 8 hours. After the completion of the reaction, the temperature was lowered to -5 ° C, 100 ml of 5N hydrochloric acid and 20 ml of water were added dropwise, and the mixture was stirred for 1 hour and then allowed to stand. The organic phase (lower layer) was separated to give 37.9 g of a colorless liquid. The purity of the gas chromatographic analysis was 99.3 %.
实施例 2  Example 2
250ml干燥三口瓶中加入 27.0g (0.20mol) 无水 A1C13, 搅拌冷至 -5°C, 滴加 20.5ml (0.20mol) 1,1, 1,3,3,3-六氟 -2-丙醇 (滴加时间 10分 钟)。 然后滴加 28.4ml (0.40mol) 二氯亚砜。 滴完后, 续搅 15分钟, 加入 9.0g (0.30mol) 低聚甲醛, 移掉冷浴, 室温搅拌白色混合物 6小 时。 反应完后, 降温至 -5 °C, 滴加 100ml 5N盐酸和 40ml水, 搅拌 1 小时后静置。 分离有机相 (下层), 得 37.2g无色液体, 收率为 87.2%。 气相色谱分析其纯度为 98.2 %。 27.0 g (0.20 mol) of anhydrous A1C1 3 was added to a 250 ml dry three-necked flask, and the mixture was cooled to -5 ° C with stirring, and 20.5 ml (0.20 mol) of 1,1,1,3,3,3-hexafluoro-2- was added dropwise. Propanol (addition time 10 minutes). Then, 28.4 ml (0.40 mol) of thionyl chloride was added dropwise. After the completion of the dropwise addition, the mixture was continuously stirred for 15 minutes, 9.0 g (0.30 mol) of paraformaldehyde was added, the cooling bath was removed, and the white mixture was stirred at room temperature for 6 hours. After the reaction, the temperature was lowered to -5 ° C, 100 ml of 5N hydrochloric acid and 40 ml of water were added dropwise, and the mixture was stirred for 1 hour and then allowed to stand. The organic phase (lower layer) was separated to give 37.2 g of a colorless liquid. The purity was 98.2% by gas chromatography.
实施例 3  Example 3
250ml 干燥三口瓶中加入 27.5g ( 0.20mol ) 无水 PC13和 0.75g ( O.Olmol ) KC1, 搅拌冷至 -5°C, 滴加 20.5ml (0.20mol ) 1,1,1,3,3,3- 六氟 -2-丙醇 (滴加时间 10分钟)。 滴完后, 续搅 15分钟, 加入 9.0g (0.30mol) 低聚甲醛, 移掉冷浴, 室温搅拌白色混合物 8小时。 反应 完后, 降温至 -5 °C, 滴加 150ml 5N盐酸和 20ml水, 搅拌 1小时后静 置。 分离有机相 (下层), 得 37.9g无色液体, 收率为 88.1 %。 气相色 谱分析其纯度为 99.3 %。 实施例 4 27.5 g (0.20 mol) of anhydrous PC1 3 and 0.75 g (O.Olmol) KC1 were added to a 250 ml dry three-necked flask, and the mixture was cooled to -5 ° C with stirring, and 20.5 ml (0.20 mol ) of 1,1,1,3 was added dropwise. 3,3-Hexafluoro-2-propanol (addition time 10 minutes). After the completion of the dropwise addition, the mixture was continuously stirred for 15 minutes, 9.0 g (0.30 mol) of paraformaldehyde was added, the cooling bath was removed, and the white mixture was stirred at room temperature for 8 hours. Reaction After completion, the temperature was lowered to -5 ° C, 150 ml of 5N hydrochloric acid and 20 ml of water were added dropwise, and the mixture was stirred for 1 hour and then allowed to stand. The organic phase (lower layer) was separated to give 37.9 g of a colourless liquid. The purity was 99.3 % by gas chromatography. Example 4
1000ml 干燥三口瓶中加入 86.3g (0.65mol ) 无水 A1C13和 1.2g (0.02mol)氯化钠,搅拌冷至 -10°C,滴加 58.9ml (0.56mol) 1,1,1,3,3,3- 六氟 -2-丙醇 (滴加时间 20分钟)。 滴完后, 续搅 30分钟, 加入 19.6g (0.65mol) 低聚甲醛, 移掉冷浴, 室温搅拌白色混合物 8小时。 反应 完后, 降温至 -10 °C, 滴加 150ml 6N盐酸和 100ml水, 搅拌 1小时后 静置。 分离有机相 (下层), 得 105.2g无色液体, 收率为 87.8% , 气相 色谱分析其纯度为 98.6%。 实施例 5 86.3 g (0.65 mol) of anhydrous A1C1 3 and 1.2 g (0.02 mol) of sodium chloride were added to a 1000 ml dry three-necked flask, and the mixture was cooled to -10 ° C with stirring, and 58.9 ml (0.56 mol) of 1,1,1,3 was added dropwise. , 3,3-hexafluoro-2-propanol (addition time 20 minutes). After the completion of the dropwise addition, the mixture was continuously stirred for 30 minutes, 19.6 g (0.65 mol) of paraformaldehyde was added, the cooling bath was removed, and the white mixture was stirred at room temperature for 8 hours. After completion of the reaction, the temperature was lowered to -10 ° C, 150 ml of 6N hydrochloric acid and 100 ml of water were added dropwise, and the mixture was stirred for 1 hour and then allowed to stand. The organic phase (lower layer) was separated to give 105.2 g of a colorless liquid with a yield of 87.8% and a purity of 98.6% by gas chromatography. Example 5
1000ml干燥三口瓶中加入 lOO.lg (0.75mol) 无水 A1C13和 1.4g1000.lg (0.75mol) anhydrous A1C1 3 and 1.4g were added to a 1000 ml dry three-necked flask.
(O.Olmol)硫酰氯,搅拌冷至 -10°C,滴加 59.3ml (0.56mol) 1,1,1,3,3,3- 六氟 -2-丙醇 (滴加时间 30分钟)。 滴完后, 续搅 30分钟, 加入 61.3g (0.29mol) 1,3,5-三氧杂环己垸, 移掉冷浴, 室温搅拌混合物 8小时。 反应完后, 降温至 -10 °C, 滴加 200ml 6N盐酸和 200ml水, 搅拌 1小 时后静置。 分离有机相 (下层), 得 107.8g无色液体, 收率为 89.1% , 采用气相色谱分析其纯度为 98.5%。 实施例 6 (O.Olmol) sulfuryl chloride, cooled to -10 ° C with stirring, and added 59.3 ml (0.56 mol) of 1,1,1,3,3,3-hexafluoro-2-propanol (dropping time 30 minutes) . After the completion of the dropwise addition, the mixture was continuously stirred for 30 minutes, 61.3 g (0.29 mol) of 1,3,5-trioxinium was added, the cooling bath was removed, and the mixture was stirred at room temperature for 8 hours. After the reaction, the temperature was lowered to -10 ° C, 200 ml of 6N hydrochloric acid and 200 ml of water were added dropwise, and the mixture was stirred for 1 hour and then allowed to stand. The organic phase (lower layer) was separated to obtain 107.8 g of a colorless liquid with a yield of 89.1% and a purity of 98.5% by gas chromatography. Example 6
1000ml 干燥三口瓶中加入 31.3g (0.12mol ) 无水 SnCl4和 80.1 (0.60mol)无水 A1C13,搅拌冷至 -5°C,滴加 60.0mK0.56mol) 1,1, 1,3,3,3- 六氟 -2-丙醇 (滴加时间 30分钟)。 滴完后, 续搅 30分钟, 加入 25.5g (0.85mol)低聚甲醛, 移掉冷浴, 室温搅拌混合物 6小时。 反应完后, 降温至 -5 °C, 滴加 200ml 6N盐酸和 200ml水, 搅拌 1小时后静置。 分 离有机相 (下层), 得 106.6g无色液体, 收率为 88.1%, 采用气相色谱 分析其纯度为 98.2%。 1000ml干燥三口瓶中加入 75.0g (0.56mol) 无水 A1C13和 48.0g ( 1.12mol) LiCl, 搅拌冷至 -5°C, 滴加 59.2ml (0.56mol ) 1,1,1,3,3,3- 六氟 -2-丙醇 (滴加时间 25分钟)。 滴完后, 续搅 30分钟, 加入 15.0g (0.65mol)低聚甲醛, 移掉冷浴, 室温搅拌混合物 6小时。 反应完后, 降温至 -5 °C, 滴加 200ml 5N盐酸和 150ml水, 搅拌 1小时后静置。 分 离有机相 (下层), 得 107.7g无色液体, 收率为 88.9%。 气相色谱分析 其纯度为 98.5%。 实施例 8 Add 31.3 g (0.12 mol) of anhydrous SnCl 4 and 80.1 (0.60 mol) of anhydrous A1C1 3 to a 1000 ml dry three-necked flask, and cool to -5 ° C with stirring, and add 60.0 mK 0.56 mol) 1,1, 1,3. 3,3-Hexafluoro-2-propanol (addition time 30 minutes). After the completion of the dropwise addition, the mixture was continuously stirred for 30 minutes, 25.5 g (0.85 mol) of paraformaldehyde was added, the cooling bath was removed, and the mixture was stirred at room temperature for 6 hours. After completion of the reaction, the temperature was lowered to -5 ° C, 200 ml of 6N hydrochloric acid and 200 ml of water were added dropwise, and the mixture was stirred for 1 hour and then allowed to stand. The organic phase (lower layer) was separated to obtain 106.6 g of a colorless liquid. The yield was 88.1%, and the purity was 98.2% by gas chromatography. 75.0 g (0.56 mol) of anhydrous A1C1 3 and 48.0 g (1.12 mol) of LiCl were added to a 1000 ml dry three-necked flask, and the mixture was cooled to -5 ° C with stirring, and 59.2 ml (0.56 mol ) of 1,1,1,3,3 was added dropwise. , 3-hexafluoro-2-propanol (addition time 25 minutes). After the completion of the dropwise addition, the mixture was continuously stirred for 30 minutes, 15.0 g (0.65 mol) of paraformaldehyde was added, the cooling bath was removed, and the mixture was stirred at room temperature for 6 hours. After the completion of the reaction, the temperature was lowered to -5 ° C, 200 ml of 5N hydrochloric acid and 150 ml of water were added dropwise, and the mixture was stirred for 1 hour and then allowed to stand. The organic phase (lower layer) was separated to give 107.7 g of a colorless liquid. The purity was 98.5% by gas chromatography. Example 8
1000ml干燥三口瓶中加入 87.0g (0.66mol) 无水 A1C13搅拌冷至 -10°C, 滴加 20.6ml (0.2mol) 1,1, 1,3,3,3-六氟 -2-丙醇 (滴加时间 10分 钟)。 然后滴加 60.2ml (0.5mol)二氯亚砜。 滴完后, 续搅 30分钟, 加 入 30.0g ( l.Omol) 低聚甲醛, 移掉冷浴, 室温搅拌混合物 8小时。 反 应完后, 降温至 -5 °C, 滴加 150ml 6N盐酸和 200ml水, 搅拌 1小时后 静置。 分离有机相 (下层), 得 38.0g无色液体, 收率为 88.3% , 采用 气相色谱分析其纯度为 98.8%。 实施例 9 87.0 g (0.66 mol) of anhydrous A1C1 3 was added to a 1000 ml dry three-necked flask, stirred and cooled to -10 ° C, and 20.6 ml (0.2 mol) of 1,1,1,3,3,3-hexafluoro-2-prop was added dropwise. Alcohol (addition time 10 minutes). Then 60.2 ml (0.5 mol) of thionyl chloride was added dropwise. After the completion of the dropwise addition, the mixture was continuously stirred for 30 minutes, 30.0 g (1.0 mol) of paraformaldehyde was added, the cooling bath was removed, and the mixture was stirred at room temperature for 8 hours. After the completion of the reaction, the temperature was lowered to -5 ° C, 150 ml of 6N hydrochloric acid and 200 ml of water were added dropwise, and the mixture was stirred for 1 hour and then allowed to stand. The organic phase (lower layer) was separated to obtain 38.0 g of a colorless liquid, yield: 88.3%, and the purity was 98.8% by gas chromatography. Example 9
1000ml干燥三口瓶中加入 134.0g ( l.Omol) 无水 A1C13和 240.6mlAdd 14.0 g (1.0 mol) of anhydrous A1C1 3 and 240.6 ml to a 1000 ml dry three-necked flask.
(2.02mol)二氯亚砜,搅拌冷至 -5°C,滴加 20.5ml (0.20mol) 1,1, 1,3,3,3- 六氟 -2-丙醇 (滴加时间 10分钟)。 滴完后, 续搅 30分钟, 加入 25.0g (0.84mol)低聚甲醛, 移掉冷浴, 室温搅拌混合物 7小时。 反应完后, 降温至 -5 °C, 滴加 250ml 5N盐酸和 150ml水, 搅拌 1小时后静置。 分 离有机相 (下层), 得 37.8g无色液体, 收率为 88.0%。 气相色谱分析 其纯度为 99.1%。 实施例 10 (2.02 mol) of thionyl chloride, cooled to -5 ° C with stirring, and 20.5 ml (0.20 mol) of 1,1,1,3,3,3-hexafluoro-2-propanol was added dropwise (dropping time 10 minutes) ). After the completion of the dropwise addition, the mixture was continuously stirred for 30 minutes, 25.0 g (0.84 mol) of paraformaldehyde was added, the cooling bath was removed, and the mixture was stirred at room temperature for 7 hours. After the reaction, the temperature was lowered to -5 ° C, 250 ml of 5N hydrochloric acid and 150 ml of water were added dropwise, and the mixture was stirred for 1 hour and then allowed to stand. The organic phase (lower layer) was separated to give 37.8 g of a colorless liquid, yield: 88.0%. The purity of the gas chromatographic analysis was 99.1%. Example 10
1000ml干燥三口瓶中加入 7.5g (0.06 mol)FeCl3和 86.5g (0.65mol) 无水 A1C13, 搅拌冷至 -5°C, 滴加 60.0ml (0.56mol) 1,1, 1,3,3,3-六氟 -2- 丙醇(滴加时间 30分钟)。滴完后,续搅 30分钟,加入 25.5g (0.84mol) 低聚甲醛,移掉冷浴,室温搅拌混合物 5小时。反应完后,降温至 -5 °C, 滴加 250ml 5N盐酸和 150ml水, 搅拌 1小时后静置。 分离有机相 (下 层),得 105.7g无色液体,收率为 87.3%。气相色谱分析其纯度为 98.8%。 7.5 g (0.06 mol) of FeCl 3 and 86.5 g (0.65 mol) of anhydrous A1C1 3 were added to a 1000 ml dry three-necked flask, and the mixture was cooled to -5 ° C with stirring, and 60.0 ml (0.56 mol) of 1,1, 1,3 was added dropwise. 3,3-hexafluoro-2-propanol (addition time 30 minutes). After the completion of the dropwise addition, continue to stir for 30 minutes, add 25.5g (0.84mol) Paraformaldehyde was removed, the cold bath was removed, and the mixture was stirred at room temperature for 5 hours. After completion of the reaction, the temperature was lowered to -5 ° C, 250 ml of 5N hydrochloric acid and 150 ml of water were added dropwise, and the mixture was stirred for 1 hour and then allowed to stand. The organic phase (lower layer) was separated to give 105.7 g of a colourless liquid. The purity was 98.8% by gas chromatography.

Claims

权利要求书: Claims:
1 .一种制备氯甲基 -1,1,1,3,3,3-六氟异丙基醚的方法,由 1,1,1,3,3,3- 六氟 -2-丙醇与 1,3,5-三氧杂环己垸或低聚甲醛反应生成, 其特征在于: 所述反应在以无水氯化路易斯酸为主催化剂, 含氯化合物为助催化剂 的二元催化体系中进行。  CLAIMS 1. A process for the preparation of chloromethyl-1,1,1,3,3,3-hexafluoroisopropyl ether from 1,1,1,3,3,3-hexafluoro-2-propanol Formed by reacting with 1,3,5-trioxanthene or paraformaldehyde, characterized in that: the reaction is a binary catalyst mainly composed of an anhydrous anhydrous Lewis acid and a chlorine-containing compound as a cocatalyst. In progress.
2. 根据权利要求 1所述的方法, 其特征在于: 所述氯化路易斯酸 和含氯化合物的摩尔比为 1 :0.01至 1 :5。 2. The method according to claim 1, wherein the molar ratio of the chlorinated Lewis acid to the chlorine-containing compound is from 1:0.01 to 1:5.
3. 根据权利要求 1所述的方法, 其特征在于: 所述氯化路易斯酸 和含氯化合物的摩尔比为 1 :0.01至 1 :2。  3. The method according to claim 1, wherein the molar ratio of the Lewis acid chloride to the chlorine-containing compound is from 1:0.01 to 1:2.
4. 根据权利要求 1 所述的方法, 其特征在于: 1,1,1,3,3,3-六氟 -2- 丙醇与 1,3,5-三氧杂环己垸或低聚甲醛的摩尔比为 1: 0.5 至 1 :5。  4. The method according to claim 1, wherein: 1,1,1,3,3,3-hexafluoro-2-propanol and 1,3,5-trioxanthene or oligomerization The molar ratio of formaldehyde is 1:0.5 to 1:5.
5. 根据权利要求 1所述的方法, 其特征在于: 1,1,1,3,3,3-六氟 -2- 丙醇与 1,3,5-三氧杂环己垸或低聚甲醛的摩尔比为 1: 0.5 至 1 :2。  The method according to claim 1, wherein: 1,1,1,3,3,3-hexafluoro-2-propanol and 1,3,5-trioxanthene or oligomerization The molar ratio of formaldehyde is 1:0.5 to 1:2.
6. 根据权利要求 2所述的方法, 其特征在于: 1,1,1,3,3,3-六氟 -2- 丙醇与氯化路易斯酸的摩尔比为 1: 0.1 至 1 :5。  The method according to claim 2, wherein the molar ratio of 1,1,1,3,3,3-hexafluoro-2-propanol to the Lewis acid chloride is 1:0.1 to 1:5. .
7. 根据权利要求 2所述的方法, 其特征在于: 1,1,1,3,3,3-六氟 -2- 丙醇与氯化路易斯酸的摩尔比为 1 : 0.1 至 1 :2。  7. The method according to claim 2, wherein the molar ratio of 1,1,1,3,3,3-hexafluoro-2-propanol to the Lewis acid chloride is 1: 0.1 to 1:2. .
8. 根据权利要求 1-7任何一项所述的方法, 其特征在于: 所述氯 化路易斯酸选自三氯化磷、 三氯化铝、 三氯化铁或四氯化锡。  The method according to any one of claims 1 to 7, wherein the chlorinated Lewis acid is selected from the group consisting of phosphorus trichloride, aluminum trichloride, iron trichloride or tin tetrachloride.
9. 根据权利要求 1-7任何一项所述的方法, 其特征在于: 所述含 氯化合物选自氯化钠、 氯化钾、 氯化锂、 二氯亚砜、 硫酰氯或三氯化 铝。 9. The method according to any one of claims 1 to 7, wherein the chlorine-containing compound is selected from the group consisting of sodium chloride, potassium chloride, lithium chloride, thionyl chloride, sulfuryl chloride or trichlorination. aluminum.
10. 根据权利要求 1-9任何一项所述的方法, 其特征在于: 所述反 应的反应时间为 5至 8小时。 10. A method according to any one of claims 1-9, characterized in that the reaction time of the reaction is 5 to 8 hours.
PCT/CN2009/070530 2008-11-17 2009-02-25 A method for preparing chloromethyl-1,1,1,3,3,3- hexafluoroisopropyl ether WO2010054540A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN200810177637.2 2008-11-17
CN200810177637A CN101735026A (en) 2008-11-17 2008-11-17 Method for preparing chloromethyl-1,1,1,3,3,3-hexafluoro isopropyl ether

Publications (1)

Publication Number Publication Date
WO2010054540A1 true WO2010054540A1 (en) 2010-05-20

Family

ID=42169608

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2009/070530 WO2010054540A1 (en) 2008-11-17 2009-02-25 A method for preparing chloromethyl-1,1,1,3,3,3- hexafluoroisopropyl ether

Country Status (2)

Country Link
CN (1) CN101735026A (en)
WO (1) WO2010054540A1 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110841663B (en) * 2019-11-25 2022-06-28 陕西煤业化工技术研究院有限责任公司 Catalyst for synthesizing anisole by taking phenol and dimethyl carbonate as raw materials, preparation method and application
CN113943214B (en) * 2021-11-11 2023-12-19 福建海西联合药业有限公司 Process for producing sevoflurane

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101058533A (en) * 2006-12-30 2007-10-24 上海沪梅化工科技发展有限公司 Method of synthesizing fluoromethyl-1,1,1,3,3,3-hexafluoroisopropyl ether

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101058533A (en) * 2006-12-30 2007-10-24 上海沪梅化工科技发展有限公司 Method of synthesizing fluoromethyl-1,1,1,3,3,3-hexafluoroisopropyl ether

Also Published As

Publication number Publication date
CN101735026A (en) 2010-06-16

Similar Documents

Publication Publication Date Title
EP1277724B1 (en) Method of preparing monofluoromethyl ethers
US8076505B2 (en) Process of preparing derivatives of 1-(2-halobiphenyl-4-yl)-cyclopropanecarboxylic acid
JPH0615485B2 (en) Method for producing polyfluorinated ether
EP2069278B1 (en) Process for the preparation of chloromethyl 2,2,2-trifluoro-1-(trifluoromethyl) ethyl ether
WO2010000136A1 (en) Method of synthesizing sevoflurane
AU2005306473B2 (en) Process for production of 1,2,2,2-tetrafluoro ethyl difluoro methyl ether
WO2010096959A1 (en) A process for preparing chloromethyl-1,1,1,3,3,3- hexafluoroisopropyl ether
WO2010054540A1 (en) A method for preparing chloromethyl-1,1,1,3,3,3- hexafluoroisopropyl ether
JPH0687777A (en) Synthesis of desflurane
JP2008162902A (en) Method for producing difluoroacetic acid ester
JP3840261B2 (en) 2,3-Dihalogeno-6-trifluoromethylbenzene derivative and method for producing the same
CN107250097A (en) The practical manufacture method of fluorine-containing α keto carboxylic acids esters
KR20030007751A (en) Method for fluoromethylation of alcohols via halogenative decarboxylation
TW201100365A (en) A process for preparing chloromethyl-1,1,1,3,3,3-hexafluoroisopropyl ether
JPH03287551A (en) Preparation of perfluoroalkyl bromide
JP2628842B2 (en) New fluorobenzotrichloride compounds
JP3057146B2 (en) Method for producing 2-halogeno-4,5-difluorobenzoyl fluorides
JPH0149338B2 (en)
JPH09188659A (en) Production of aromatic nitrile compound containing halogen
JP2008120763A (en) Method for producing fluorine-containing allyl compound and method for producing fluorine-containing epoxy compound
TW201245133A (en) Process for the manufacture of fluoromethoxymalonic acid derivatives
JPH085809B2 (en) Process for producing nuclear fluorinated benzoyl fluoride compound
JPH0713043B2 (en) 3,4-Dichloro-6-trifluoromethyl-toluene derivative and process for producing the same

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 09825715

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 09825715

Country of ref document: EP

Kind code of ref document: A1