WO2007142266A1 - Method for producing fluorinated fluorosulfonylalkyl vinyl ether - Google Patents

Method for producing fluorinated fluorosulfonylalkyl vinyl ether Download PDF

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WO2007142266A1
WO2007142266A1 PCT/JP2007/061456 JP2007061456W WO2007142266A1 WO 2007142266 A1 WO2007142266 A1 WO 2007142266A1 JP 2007061456 W JP2007061456 W JP 2007061456W WO 2007142266 A1 WO2007142266 A1 WO 2007142266A1
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fluorine
weight
parts
vinyl ether
chemical formula
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PCT/JP2007/061456
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French (fr)
Japanese (ja)
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Yuuichi Hashikawa
Akinari Sugiyama
Kazuyoshi Ichihara
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Daikin Industries, Ltd.
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Publication of WO2007142266A1 publication Critical patent/WO2007142266A1/en

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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C303/00Preparation of esters or amides of sulfuric acids; Preparation of sulfonic acids or of their esters, halides, anhydrides or amides
    • C07C303/02Preparation of esters or amides of sulfuric acids; Preparation of sulfonic acids or of their esters, halides, anhydrides or amides of sulfonic acids or halides thereof
    • C07C303/22Preparation of esters or amides of sulfuric acids; Preparation of sulfonic acids or of their esters, halides, anhydrides or amides of sulfonic acids or halides thereof from sulfonic acids, by reactions not involving the formation of sulfo or halosulfonyl groups; from sulfonic halides by reactions not involving the formation of halosulfonyl groups

Definitions

  • the present invention relates to a method for producing a fluorine-containing fluorosulfoalkyl alkyl ether.
  • the fluorine-containing fluorosulfoalkyl alkyl ether is a useful compound as an industrial raw material such as an ion exchange membrane material.
  • FC0CF (CF) 0CF CF SO F is used as a raw material, and its cyclized product
  • a method for converting to 3 2 2 2 2 2 groups is also known (see Patent Document 2 below).
  • CF CFO (CF CF (CF) 0) CF CF SO CI (where n is 0 or 1)
  • a fluorine-containing fluorosulfoalkyl alkyl ether can be obtained by reacting with a fluorine-containing agent using water as a solvent when the fluorine-containing chlorosulfoalkyl alkyl ether is used as a starting material (see below).
  • Patent Document 3 the target fluorine-containing fluorosulfoalkyl alkyl ether can be obtained in a relatively high yield, but HF adducts and hydrolysates are produced as by-products.
  • a method capable of producing a target fluorine-containing fluorosulfoalkyl vinyl ether with higher selectivity and good yield is desired.
  • Patent Document 1 British Patent 1, 034, 197
  • Patent Document 2 U.S. Pat.No. 3,560,568
  • Patent Document 3 Japanese Patent Application Laid-Open No. 2004-244401
  • Non-Patent Document 1 S. Benefice—Malouet, H. Blancou, R. Teissedre and A. Commeyras, J. Fluorine Chem. 31 (1986) 319—332
  • the present invention has been made in view of the current state of the prior art described above, and the main object of the present invention is to easily and highly select fluorine-containing fluorosulfoalkyl alkyl ethers in an industrially advantageous manner. It is to provide a method that can be manufactured at a high yield with a high yield.
  • the inventor has conducted extensive research in view of the above-described problems. As a result, when a specific fluorine-containing chlorosulfoalkylalkyl ether was used as a raw material and reacted with a fluorinating agent, it was very limited to 0.05 to 9 parts by weight per 100 parts by weight of the raw material. Surprisingly, when a small amount of water is present, the selectivity is significantly improved and by-products are much less pure and highly pure than when water is used as a solvent or without water. The inventors have found that it is possible to obtain a fluorinated fluorosulfoalkyl alkyl ether, and have completed the present invention.
  • the present invention provides the following method for producing a fluorine-containing fluorosulfoalkyl alkyl ether.
  • Fluorine-containing chlorosulfoalkyl alkyl butyl ether represented by the following formula: MF '(HF) (wherein M is an alkali metal and X is 0 to 5)
  • MF '(HF) wherein M is an alkali metal and X is 0 to 5
  • CF CF (CF) 0 (CF CF (C)
  • a method for producing hole alkyl butyl ether comprising reacting in the presence of 0.05 to 9 parts by weight of water per 100 parts by weight of fluorine-containing chloroalkyl sulfone ether used as a raw material.
  • Key formula: CF CF (CF) 0 (CF CF (CF) 0) (CF) SO CI! /, A force ⁇ 0, b force or
  • Fluorinating agent power The method according to item 1 or 2, which is at least one selected from the group force consisting of a compound in which M is K and M is a compound in MF- (HF).
  • fluorine-containing chlorosulfoalkyl alkyl ethers compounds in which a is 0, b is 0 or 1, and c is an integer of 1 to 4 are used as raw materials for producing monomer components for fuel cell electrolyte polymers. It is highly useful.
  • a compound represented by the chemical formula: MF ′ (HF) (wherein M is an alkali metal and X is an integer of 0 to 5) is used as the fluorinating agent.
  • the fluorinating agent an alkali metal fluoride, an acid alkali metal fluoride or the like, which is a compound in which M is K or a compound in which M is Na in the above chemical formula, is preferable.
  • KF is preferable.
  • Fluorinating agents can be used alone or in combination of two or more.
  • the amount of the fluorinating agent used is usually about 0.5 to 10 mol, preferably about 1 to 5 mol, relative to 1 mol of the fluorinated chlorosulfuralkylalkyl ether.
  • the production method of the present invention comprises the use of the above-mentioned fluorine-containing chlorosulfoalkyl alkyl ether by reacting the fluorine-containing chlorosulfoalkyl alkyl ether with a fluorinating agent.
  • An important feature is the presence of a specific amount of water of 0.05 to 9 parts by weight per 100 parts by weight of rualkyl butyl ether.
  • the reaction proceeds in the presence of a specific proportion of water, which is a small amount relative to the raw material, thereby suppressing the formation of by-products and high yield with high selectivity.
  • a specific proportion of water which is a small amount relative to the raw material, thereby suppressing the formation of by-products and high yield with high selectivity.
  • This makes it possible to obtain the target fluorine-containing fluorosulfoalkyl alkyl ether. If the presence of water exceeds the above range, the by-product will increase!] And the selectivity will decrease, and if below, the reaction time will be significantly longer.
  • the amount of water is preferably about 0.1 to 6 parts by weight with respect to 100 parts by weight of the fluorine-containing chlorosulfoalkyl alkyl butyl ether. More preferably.
  • additives can be added as required.
  • additives include water-soluble organic solvents that do not participate in the reaction, such as sulfolane, dimethyl sulfoxide, dimethylformamide, and other phase transfer catalysts such as C H
  • Quaternary ammonium salts such as CH N (CH) .C1, quaternary phosphonium salts, etc., inclusion molecules, eg
  • a cyclic ether such as 18-crown-6 can be used.
  • the reaction rate can be improved by adding these additives.
  • the amount of the additive used for the aqueous organic solvent is preferably about 1 to 50 parts by weight with respect to 100 parts by weight of the fluorine-containing chlorosulfoalkyl alkyl ether used as a raw material.
  • the phase transfer catalyst is preferably about 0.1 to 10 parts by weight with respect to 100 parts by weight of the fluorine-containing chlorosulfonylalkyl vinyl ether used as a raw material.
  • the raw material and the fluorinating agent may be reacted in the presence of the specific amount of water described above.
  • the reaction temperature may be about 10 to 200 ° C, preferably about 15 to 100 ° C.
  • the reaction pressure may be any of reduced pressure, atmospheric pressure and increased pressure, but is preferably atmospheric pressure.
  • the reaction time is usually about 0.5 to 24 hours.
  • the obtained crude compound can be purified by a known method such as distillation or column chromatography.
  • the mixture is separated into two layers by adding water and stirring, and the lower layer becomes a fluorinated fluorosulfoalkyl alkyl ether represented by the above chemical formula and can be purified by the above method.
  • the fluorine-containing fluorosulfoalkyl alkyl ether obtained as described above is a substance useful as a monomer component for a fuel cell electrolyte polymer, for example.
  • the reactor was heated with stirring and refluxed at 95 ° C. During the reaction, the reflux temperature dropped and the reaction was stopped when it became constant at 75 ° C. The total reaction time was 2 hours.
  • CF CF ⁇ CF CF SO K has a selectivity of 0.1%, CF CHFOCF C
  • F SO F was produced with a selectivity of 0.1% and CF CHFOCF CF SO K with a selectivity of 0.5%.

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

Abstract

Disclosed is a method for producing a fluorinated fluorosulfonylalkyl vinyl ether represented by the following chemical formula: CF2=CF(CF2)aO(CF2CF(CF3)O)b(CF2)cSO2F (wherein a, b and c are as defined below) by reacting a fluorinated chlorosulfonylalkyl vinyl ether represented by the following chemical formula: CF2=CF(CF2)aO(CF2CF(CF3)O)b(CF2)cSO2Cl (wherein a represents 0 or 1, b represents an integer of 0-5 and c represents an integer of 1-10) with a fluorinating agent represented by the following chemical formula: MF•(HF)x (wherein M represents an alkali metal and x represents an integer of 0-5). This method for producing a fluorinated fluorosulfonylalkyl vinyl ether is characterized in that the reaction is carried out in the presence of 0.05-9 parts by weight of water per 100 parts by weight of the fluorinated chlorosulfonylalkyl vinyl ether as a raw material. This method enables to commercially advantageously produce a fluorinated fluorosulfonylalkyl vinyl ether with high selectivity and high yield by a simple process.

Description

含フッ素フルォロスルホニルアルキルビュルエーテルの製造方法 技術分野  Technical field of production of fluorine-containing fluorosulfonylalkyl butyl ether
[0001] 本発明は、含フッ素フルォロスルホ-ルアルキルビュルエーテルの製造方法に関 する。  [0001] The present invention relates to a method for producing a fluorine-containing fluorosulfoalkyl alkyl ether.
背景技術  Background art
[0002] 化学式: CF =CFO(CF CF(CF )0) CF CF SO F (式中、 nは 0又は 1である)で表さ  [0002] Chemical formula: CF = CFO (CF CF (CF) 0) CF CF SO F (where n is 0 or 1)
2 2 3 n 2 2 2  2 2 3 n 2 2 2
れる含フッ素フルォロスルホ-ルアルキルビュルエーテルは、イオン交換膜材料など の工業原料として有用な化合物である。  The fluorine-containing fluorosulfoalkyl alkyl ether is a useful compound as an industrial raw material such as an ion exchange membrane material.
[0003] 該含フッ素フルォロスルホ-ルアルキルビュルエーテル等のスルホ-ルビ-ルエー テルの製造方法としては、例えば、へキサフルォロプロピレンォキシドを FCOCF SO  [0003] As a method for producing a sulfonylvinyl ether such as the fluorine-containing fluorosulfoalkyl alkyl ether, for example, hexafluoropropylene oxide is prepared by FCOCF SO
2 2 twenty two
Fに付加させた後、得られた酸フロリド誘導体を熱分解する方法が知られている(下記 特許文献 1参照)。し力しながら、この方法では、へキサフルォロプロピレンォキシドを 2分子以上付カ卩したものからは、 CF =CFO(CF CF(CF )0) CF CF SO Fで表されるス A method of thermally decomposing the resulting acid fluoride derivative after addition to F is known (see Patent Document 1 below). However, in this method, from the case where two or more molecules of hexafluoropropylene oxide are attached, CF = CFO (CF CF (CF) 0) CF CF SO F
2 2 3 n 2 2 2  2 2 3 n 2 2 2
ルホビュルエーテルを得ることは可能である力 へキサフルォロプロピレンォキシドを It is possible to obtain Rhebubul ether. Hexafluoropropylene oxide
1分子付加したものからは、下記式 From the addition of one molecule, the following formula
[0004] [化 1] [0004] [Chemical 1]
Figure imgf000003_0001
Figure imgf000003_0001
[0005] で表される環化体が主生成物として生じ、化学式 CF =CF0CF CF SO Fで表される [0005] A cyclized product represented by the following formula is generated as a main product, and represented by the chemical formula CF = CF0CF CF SO F
2 2 2 2  2 2 2 2
含フッ素フルォロスルホ-ルアルキルビュルエーテルをほとんど得ることができない ( Almost no fluorine-containing fluorosulfol alkyl butyl ether can be obtained (
[0006] また、 FC0CF(CF )0CF CF SO Fを原料として用い、その環化体 [0006] Further, FC0CF (CF) 0CF CF SO F is used as a raw material, and its cyclized product
3 2 2 2  3 2 2 2
[0007] [化 2] 严 [0007] [Chemical 2] 严
ヽ严2 ヽ 严2
F2C—— CF2  F2C——CF2
[0008] を形成した後、 CH ONaを用いて開環させて CF =CFOCF CF SO Naとし、その後、 [0008] is formed, then the ring is opened using CH ONa to make CF = CFOCF CF SO Na,
3 2 2 2 3  3 2 2 2 3
末端の SO Na基を塩素化して CF =CFOCF CF SO CIとし、更に、フッ素化して SO F  The terminal SO Na group is chlorinated to CF = CFOCF CF SO CI, and further fluorinated to SO F
3 2 2 2 2 2 基に変換する方法も知られて ヽる(下記特許文献 2参照)。ここに記載されて ヽるフッ 素化工程は、溶媒としてスルホランを用い、フッ素化剤として NaFを用いる方法である 力 溶媒として高融点、高沸点を有するスルホランを用いるため、反応中に分解して 生じた CF =CFOCF CF SO Naなどの有効成分や、未反応原料の NaF、副生成物で  A method for converting to 3 2 2 2 2 2 groups is also known (see Patent Document 2 below). The fluorination step described here uses sulfolane as the solvent and NaF as the fluorinating agent. Because it uses a sulfolane having a high melting point and a high boiling point as the solvent, it is decomposed during the reaction. Generated active ingredients such as CF = CFOCF CF SO Na, unreacted raw material NaF, and by-products
2 2 2 3  2 2 2 3
ある NaClとの分離が困難であり、スルホランと固体の有効成分を回収する工程が非 常に複雑となる。このため、この方法は、工業的実施は困難であり、産業廃棄物が多 量に生じるという問題もある。  Separation from certain NaCl is difficult, and the process of recovering sulfolane and the solid active ingredient becomes very complicated. For this reason, this method is difficult to implement industrially and there is a problem that a large amount of industrial waste is generated.
[0009] その他に、含フッ素スルホン酸クロリドのフッ素化方法としては、パーフルォロアルキ ル基を有する化合物である C F SO C1を原料とする場合には、 KFを用いてフッ素化 [0009] In addition, as a method for fluorinating a fluorine-containing sulfonic acid chloride, when C F SO C1, which is a compound having a perfluoroalkyl group, is used as a raw material, fluorination is performed using KF.
8 17 2  8 17 2
することにより C F SO Fが得られることが報告されている(下記非特許文献 1参照)。  It has been reported that C 2 F 3 SO F can be obtained (see Non-Patent Document 1 below).
8 17 2  8 17 2
この方法では、高収率でフッ素化物を得るためには、スルホラン、ホルムアミドなどを 溶媒として用いることが必要であり、単純な反応系が期待できる水を溶媒とした場合 には、 100°Cでフッ素化しても、 C F SO Fの収率は 25%程度に過ぎず、工業的実  In this method, it is necessary to use sulfolane, formamide, or the like as a solvent in order to obtain a fluorinated product in a high yield. When water is used as a solvent, which can be expected to be a simple reaction system, the solvent is used at 100 ° C. Even with fluorination, the yield of CF SO F is only about 25%.
8 17 2  8 17 2
施化には不適切である。  Unsuitable for application.
[0010] 更に、 CF =CFO(CF CF(CF )0) CF CF SO CI (式中、 nは 0又は 1である)で表され [0010] Further, CF = CFO (CF CF (CF) 0) CF CF SO CI (where n is 0 or 1)
2 2 3 n 2 2 2  2 2 3 n 2 2 2
る含フッ素クロロスルホ -ルアルキルビュルエーテルを出発原料とする場合に、水を 溶媒としてフッ素ィ匕剤と反応させることにより、含フッ素フルォロスルホ-ルアルキル ビュルエーテルを得ることができることが報告されている(下記特許文献 3参照)。この 方法によれば、 目的とする含フッ素フルォロスルホ-ルアルキルビュルエーテルを比 較的高収率で得ることが可能であるが、副生成物として、 HF付加体、加水分解物な どが生じるために、より高い選択率で収率良く目的とする含フッ素フルォロスルホ- ルアルキルビニルエーテルを製造可能な方法が望まれる。 特許文献 1 :英国特許 1, 034, 197号 It has been reported that a fluorine-containing fluorosulfoalkyl alkyl ether can be obtained by reacting with a fluorine-containing agent using water as a solvent when the fluorine-containing chlorosulfoalkyl alkyl ether is used as a starting material (see below). (See Patent Document 3). According to this method, the target fluorine-containing fluorosulfoalkyl alkyl ether can be obtained in a relatively high yield, but HF adducts and hydrolysates are produced as by-products. In addition, a method capable of producing a target fluorine-containing fluorosulfoalkyl vinyl ether with higher selectivity and good yield is desired. Patent Document 1: British Patent 1, 034, 197
特許文献 2 :米国特許第 3, 560, 568号  Patent Document 2: U.S. Pat.No. 3,560,568
特許文献 3:特開 2004 - 244401号公報  Patent Document 3: Japanese Patent Application Laid-Open No. 2004-244401
非特許文献 1 : S. Benefice— Malouet, H. Blancou, R. Teissedre and A. Commeyras, J. Fluorine Chem. 31 (1986) 319— 332  Non-Patent Document 1: S. Benefice—Malouet, H. Blancou, R. Teissedre and A. Commeyras, J. Fluorine Chem. 31 (1986) 319—332
発明の開示 発明が解決しょうとする課題  Disclosure of the Invention Problems to be Solved by the Invention
[0011] 本発明は、上記した従来技術の現状に鑑みてなされたものであり、その主な目的は 、含フッ素フルォロスルホ-ルアルキルビュルエーテルを、工業的に有利な方法で、 簡便に高い選択率で収率良く製造できる方法を提供することである。 [0011] The present invention has been made in view of the current state of the prior art described above, and the main object of the present invention is to easily and highly select fluorine-containing fluorosulfoalkyl alkyl ethers in an industrially advantageous manner. It is to provide a method that can be manufactured at a high yield with a high yield.
課題を解決するための手段  Means for solving the problem
[0012] 本発明者は、上記した問題点に鑑みて鋭意研究を重ねてきた。その結果、特定の 含フッ素クロロスルホ -ルアルキルビュルエーテルを原料として用い、これをフッ素化 剤と反応させる際に、原料 100重量部に対して 0. 05〜9重量部という非常に限定さ れた少量の水を存在させる場合には、驚くべきことに、水を溶媒とする場合や水を用 いない場合と比較して、選択率が顕著に向上し、副生成物が非常に少なく高純度の 含フッ素フルォロスルホ-ルアルキルビュルエーテルを得ることが可能となることを見 出し、ここに本発明を完成するに至った。 [0012] The inventor has conducted extensive research in view of the above-described problems. As a result, when a specific fluorine-containing chlorosulfoalkylalkyl ether was used as a raw material and reacted with a fluorinating agent, it was very limited to 0.05 to 9 parts by weight per 100 parts by weight of the raw material. Surprisingly, when a small amount of water is present, the selectivity is significantly improved and by-products are much less pure and highly pure than when water is used as a solvent or without water. The inventors have found that it is possible to obtain a fluorinated fluorosulfoalkyl alkyl ether, and have completed the present invention.
[0013] 即ち、本発明は、下記の含フッ素フルォロスルホ-ルアルキルビュルエーテルの製 造方法を提供するものである。 That is, the present invention provides the following method for producing a fluorine-containing fluorosulfoalkyl alkyl ether.
1. ィ匕学式: CF =CF(CF ) 0(CF CF(CF )0) (CF ) SO Cl(式中、 aは 0又は 1、 bは 0  1. Formulas: CF = CF (CF) 0 (CF CF (CF) 0) (CF) SO Cl (where a is 0 or 1, b is 0
2 2 a 2 3 b 2 c 2  2 2 a 2 3 b 2 c 2
〜5の整数、 cは 1〜10の整数である)で表される含フッ素クロロスルホ -ルアルキル ビュルエーテルと化学式: MF'(HF) (式中、 Mはアルカリ金属であり、 Xは 0〜5の整 数である)で表されるフッ素ィ匕剤とを反応させて、化学式: CF =CF(CF ) 0(CF CF(C  Fluorine-containing chlorosulfoalkyl alkyl butyl ether represented by the following formula: MF '(HF) (wherein M is an alkali metal and X is 0 to 5) The chemical formula: CF = CF (CF) 0 (CF CF (C
2 2 a 2 2 2 a 2
F )0) (CF ) SO F (式中、 a、 b及び cは上記に同じ)で表される含フッ素フルォロスルF) 0) (CF) SO F (wherein a, b and c are the same as above)
3 b 2 c 2 3 b 2 c 2
ホ-ルアルキルビュルエーテルを製造する方法であって、原料とする含フッ素クロ口 スルホ-ルアルキルビュルエーテル 100重量部に対して 0. 05〜9重量部の水の存 在下に反応を行うことを特徴とする方法。 2. ィ匕学式: CF =CF(CF ) 0(CF CF(CF )0) (CF ) SO CIにお!/、て、 a力 ^0、 b力 又 A method for producing hole alkyl butyl ether, comprising reacting in the presence of 0.05 to 9 parts by weight of water per 100 parts by weight of fluorine-containing chloroalkyl sulfone ether used as a raw material. A method characterized by. 2. Key formula: CF = CF (CF) 0 (CF CF (CF) 0) (CF) SO CI! /, A force ^ 0, b force or
2 2 a 2 3 b 2 c 2  2 2 a 2 3 b 2 c 2
は 1、 cが 1〜4の整数である含フッ素クロロスルホ -ルアルキルビュルエーテルを原 料として用いる上記項 1に記載の方法。  2. The method according to item 1, wherein fluorinated chlorosulfoalkyl alkyl butyl ether in which 1, c is an integer of 1 to 4 is used as a raw material.
3. フッ素化剤力 化学式: MF-(HF)において Mが Kの化合物及び Mが Naの化合 物からなる群力 選ばれた少なくとも一種である上記項 1又は 2に記載の方法。  3. Fluorinating agent power The method according to item 1 or 2, which is at least one selected from the group force consisting of a compound in which M is K and M is a compound in MF- (HF).
4. 原料とする含フッ素クロロスルホ -ルアルキルビュルエーテル 100重量部に対し て 0. 1〜6重量部の水の存在下に反応を行う上記項 1〜3のいずれかに記載の方法  4. The method according to any one of the above items 1 to 3, wherein the reaction is carried out in the presence of 0.1 to 6 parts by weight of water with respect to 100 parts by weight of the fluorine-containing chlorosulfuralkylalkyl ether used as a raw material.
[0014] 本発明の含フッ素フルォロスルホ-ルアルキルビュルエーテルの製造方法は、ィ匕 学式: CF =CF(CF ) 0(CF CF(CF )0) (CF ) SO Cl(式中、 aは 0又は 1、 bは 0〜5の [0014] The method for producing a fluorine-containing fluorosulfol alkyl butyl ether of the present invention has the following chemical formula: CF = CF (CF) 0 (CF CF (CF) 0) (CF) SO Cl (where a is 0 or 1, b is 0-5
2 2 a 2 3 b 2 c 2  2 2 a 2 3 b 2 c 2
整数、 cは 1〜10の整数である)で表される含フッ素クロロスルホ -ルアルキルビュル エーテルと、化学式: MF-(HF) (式中、 Mはアルカリ金属であり Xは 0〜5の整数であ る)で表されるフッ素ィ匕剤とを反応させて、ィ匕学式: CF =CF(CF ) 0(CF CF(CF )0) (  Fluorine-containing chlorosulfuralkylalkyl ether represented by an integer, c is an integer of 1 to 10, and a chemical formula: MF- (HF) (wherein M is an alkali metal and X is an integer of 0 to 5) Is expressed by the following formula: CF = CF (CF) 0 (CF CF (CF) 0) (
2 2 a 2 3 b 2 2 a 2 3 b
CF ) SO F (式中、 a、 b及び cは上記に同じ)で表される含フッ素フルォロスルホニルCF 3) SO F (wherein a, b and c are the same as above)
2 c 2 2 c 2
アルキルビニルエーテルを製造する方法である。  This is a method for producing an alkyl vinyl ether.
[0015] 原料とする化学式: CF =CF(CF ) 0(CF CF(CF )0) (CF ) SO CI (式中、 a、 b及び c [0015] Chemical formula as a raw material: CF = CF (CF) 0 (CF CF (CF) 0) (CF) SO CI (where a, b and c
2 2 a 2 3 b 2 c 2  2 2 a 2 3 b 2 c 2
は上記に同じ)で表される含フッ素クロロスルホ -ルアルキルビュルエーテルは公知 物質であり、例えば、上記化学式において、 aが 0の化合物については、特開 2004 — 18427号公報に記載の方法により、公知物質である一般式 CFX (CF ) X (式中、 X  Is the same as the above) and is a known substance. For example, in the above chemical formula, for a compound in which a is 0, by the method described in JP-A-2004-18427, A general formula CFX (CF) X (where X
2 2  twenty two
は Iまたは Brであり、 cは 1〜10の整数である。)で表される含フッ素化合物を SO、 CIS  Is I or Br, and c is an integer of 1-10. ) Is a fluorine-containing compound represented by SO, CIS
3 Three
0 H、発煙硫酸等と反応させて FOC(CF ) X (式中、 c及び Xは上記に同じ)とした後、After reacting with 0 H, fuming sulfuric acid, etc. to make FOC (CF) X (where c and X are the same as above),
3 2 c 3 2 c
へキサフルォロプロピレンオキサイドとオリゴメリ反応を行 、、その後中和及び脱炭酸 反応を行い、 CF =CF0(CF CF(CF )0) (CF ) X (式中、 b、 c及び Xは上記に同じ)とし  Oxymeric reaction with hexafluoropropylene oxide, followed by neutralization and decarboxylation reaction, CF = CF0 (CF CF (CF) 0) (CF) X (where b, c and X are the above And the same)
2 2 3 b 2 c  2 2 3 b 2 c
、アルカリ金属の亜ジチオン酸塩及び中和剤と反応させてビュルエーテルスルフィン 酸塩とし、得られたビュルエーテルスルフィン酸塩を塩素化する方法によって得ること ができる。この方法で得られる含フッ素クロロスルホ -ルアルキルビュルエーテルは、 単離、精製したものを使用してもよぐ或いは、上記反応で得られた粗反応生成物を そのまま使用しても良い。 [0016] 本発明では、上記化学式: CF =CF(CF ) 0(CF CF(CF )0) (CF ) SO CIで表される It can be obtained by a method of reacting with an alkali metal dithionite and a neutralizing agent to form butyl ether sulfinate, and chlorinating the obtained butyl ether sulfinate. The fluorine-containing chlorosulfoalkyl alkyl ether obtained by this method may be isolated or purified, or the crude reaction product obtained by the above reaction may be used as it is. In the present invention, the chemical formula is represented by the formula: CF = CF (CF) 0 (CF CF (CF) 0) (CF) SO CI
2 2 a 2 3 b 2 c 2  2 2 a 2 3 b 2 c 2
含フッ素クロロスルホ -ルアルキルビュルエーテルの内で、特に、 aが 0、 bが 0又は 1 、 cが 1〜4の整数である化合物は、燃料電池電解質ポリマー用のモノマー成分の製 造原料としての有用性が高 、ものである。 Among the fluorine-containing chlorosulfoalkyl alkyl ethers, compounds in which a is 0, b is 0 or 1, and c is an integer of 1 to 4 are used as raw materials for producing monomer components for fuel cell electrolyte polymers. It is highly useful.
[0017] 本発明では、フッ素化剤としては、化学式: MF'(HF) (式中、 Mはアルカリ金属であ り Xは 0〜5の整数である)で表される化合物を用いる。フッ素化剤としては、上記化学 式において、 Mが Kの化合物又は Mが Naの化合物であるアルカリ金属フッ化物、酸 性フッ化アルカリ金属等が好ましい。特に、 KFが好ましい。フッ素化剤は一種単独又 は二種以上混合して用いることができる。  In the present invention, a compound represented by the chemical formula: MF ′ (HF) (wherein M is an alkali metal and X is an integer of 0 to 5) is used as the fluorinating agent. As the fluorinating agent, an alkali metal fluoride, an acid alkali metal fluoride or the like, which is a compound in which M is K or a compound in which M is Na in the above chemical formula, is preferable. In particular, KF is preferable. Fluorinating agents can be used alone or in combination of two or more.
[0018] フッ素化剤の使用量は、通常、含フッ素クロロスルホ -ルアルキルビュルエーテル 1 モルに対して 0. 5〜10モル程度とすれば良ぐ 1〜5モル程度とすることが好ましい。  [0018] The amount of the fluorinating agent used is usually about 0.5 to 10 mol, preferably about 1 to 5 mol, relative to 1 mol of the fluorinated chlorosulfuralkylalkyl ether.
[0019] 本発明の製造方法は、上記した含フッ素クロロスルホ -ルアルキルビュルエーテル とフッ素化剤とを反応させて含フッ素フルォロスルホ-ルアルキルビュルエーテルを 製造する際に、原料とする含フッ素クロロスルホ -ルアルキルビュルエーテル 100重 量部に対して、 0. 05〜9重量部という特定量の水を存在させることを重要な特徴と するものである。  [0019] The production method of the present invention comprises the use of the above-mentioned fluorine-containing chlorosulfoalkyl alkyl ether by reacting the fluorine-containing chlorosulfoalkyl alkyl ether with a fluorinating agent. An important feature is the presence of a specific amount of water of 0.05 to 9 parts by weight per 100 parts by weight of rualkyl butyl ether.
[0020] この様に、原料に対して少量であって、し力も特定の割合の水の存在下に反応を 進行させることによって、副生成物の生成を抑制して、選択性よく高収率で目的とす る含フッ素フルォロスルホ-ルアルキルビュルエーテルを得ることが可能となる。水の 存在が上記範囲を上回る場合は副生成物が増力!]して選択率が低下し、下回る場合 は反応時間が著しく長くなる。  [0020] In this manner, the reaction proceeds in the presence of a specific proportion of water, which is a small amount relative to the raw material, thereby suppressing the formation of by-products and high yield with high selectivity. This makes it possible to obtain the target fluorine-containing fluorosulfoalkyl alkyl ether. If the presence of water exceeds the above range, the by-product will increase!] And the selectivity will decrease, and if below, the reaction time will be significantly longer.
[0021] 特に、水の存在量は、含フッ素クロロスルホ -ルアルキルビュルエーテル 100重量 部に対して、 0. 1〜6重量部程度とすることが好ましぐ 0. 5〜2重量部程度とするこ とがより好ましい。 [0021] In particular, the amount of water is preferably about 0.1 to 6 parts by weight with respect to 100 parts by weight of the fluorine-containing chlorosulfoalkyl alkyl butyl ether. More preferably.
[0022] 本発明の製造方法では、更に、必要に応じて、その他の添加剤をカ卩えることができ る。この様な添加剤としては、反応に関与しない水溶性の有機溶媒、例えば、スルホ ラン、ジメチルスルホキシド、ジメチルホルムアミド等ゃ相関移動触媒、例えば、 C H  [0022] In the production method of the present invention, other additives can be added as required. Such additives include water-soluble organic solvents that do not participate in the reaction, such as sulfolane, dimethyl sulfoxide, dimethylformamide, and other phase transfer catalysts such as C H
6 5 6 5
CH N(CH ) .C1のような四級アンモニゥム塩、四級ホスホニゥム塩等、包接分子、例 えば、 18—クラウンー6のような環状エーテル等、を用いることができる。これらの添 加剤を加えることによって、反応速度を向上させることが可能である。 Quaternary ammonium salts such as CH N (CH) .C1, quaternary phosphonium salts, etc., inclusion molecules, eg For example, a cyclic ether such as 18-crown-6 can be used. The reaction rate can be improved by adding these additives.
[0023] 添加剤の使用量は、水性有機溶媒については、原料とする含フッ素クロロスルホ- ルアルキルビュルエーテル 100重量部に対して、 1〜50重量部程度とすることが好 ましい。 [0023] The amount of the additive used for the aqueous organic solvent is preferably about 1 to 50 parts by weight with respect to 100 parts by weight of the fluorine-containing chlorosulfoalkyl alkyl ether used as a raw material.
[0024] また、相間移動触媒にっ 、ては、原料とする含フッ素クロロスルホニルアルキルビ- ルエーテル 100重量部に対して、 0. 1〜10重量部程度とすることが好ましい。  [0024] The phase transfer catalyst is preferably about 0.1 to 10 parts by weight with respect to 100 parts by weight of the fluorine-containing chlorosulfonylalkyl vinyl ether used as a raw material.
[0025] 本発明の製造方法では、上記した特定量の水の存在下に、原料とフッ素化剤を反 応させれば良い。反応条件の一例としては、反応温度 10〜200°C程度、好ましくは 1 5〜100°C程度とすればよい。反応圧力については、減圧、大気圧、加圧のいずれ でもよいが、大気圧とすることが好ましい。反応時間は、通常 0. 5〜24時間程度であ る。  In the production method of the present invention, the raw material and the fluorinating agent may be reacted in the presence of the specific amount of water described above. As an example of the reaction conditions, the reaction temperature may be about 10 to 200 ° C, preferably about 15 to 100 ° C. The reaction pressure may be any of reduced pressure, atmospheric pressure and increased pressure, but is preferably atmospheric pressure. The reaction time is usually about 0.5 to 24 hours.
[0026] 以上の方法によって、化学式: CF =CF(CF ) 0(CF CF(CF )0) (CF ) SO F (式中、  [0026] By the above method, the chemical formula: CF = CF (CF) 0 (CF CF (CF) 0) (CF) SO F (wherein
2 2 a 2 3 b 2 c 2 a、 b及び cは上記に同じ)で表される含フッ素フルォロスルホ-ルアルキルビュルエー テルを得ることができる。  2 2 a 2 3 b 2 c 2 a, b and c are the same as above, and a fluorinated fluorosulfoalkyl alkyl ether can be obtained.
[0027] 得られた粗ィ匕合物は、蒸留、カラムクロマトグラフィーなどの公知の方法で精製でき る。例えば、水を加えて撹拌することによって二層に分液し、下層は、上記化学式で 表される含フッ素フルォロスルホ-ルアルキルビュルエーテルとなり、上記の方法で 精製することができる。 [0027] The obtained crude compound can be purified by a known method such as distillation or column chromatography. For example, the mixture is separated into two layers by adding water and stirring, and the lower layer becomes a fluorinated fluorosulfoalkyl alkyl ether represented by the above chemical formula and can be purified by the above method.
[0028] この様にして得られる含フッ素フルォロスルホ-ルアルキルビュルエーテルは、例 えば、燃料電池電解質ポリマー用のモノマー成分等として有用な物質である。  [0028] The fluorine-containing fluorosulfoalkyl alkyl ether obtained as described above is a substance useful as a monomer component for a fuel cell electrolyte polymer, for example.
発明の効果  The invention's effect
[0029] 本発明の製造方法によれば、比較的簡単な製造方法によって、非常に高い選択率 で収率良く含フッ素フルォロスルホ-ルアルキルビュルエーテルを製造することがで きる。  [0029] According to the production method of the present invention, it is possible to produce a fluorine-containing fluorosulfoalkyl alkyl ether with a very high selectivity and high yield by a relatively simple production method.
[0030] 従って、本発明の製造方法によれば、収率向上に伴うコストダウンが可能であり、更 に、産業廃棄物の低減、製造装置の腐食の抑制、製造工程の簡略ィヒなどの優れた 効果が発揮される。 図面の簡単な説明 [0030] Therefore, according to the production method of the present invention, it is possible to reduce the cost accompanying the improvement in yield, and further, such as reduction of industrial waste, suppression of corrosion of production equipment, simplification of production process, etc. Excellent effect. Brief Description of Drawings
[0031] [図 1]CF =CFO CF CF SO F選択率と、 CF =CFOCF CF SO CI 100重量部に対す  [0031] [Fig. 1] CF = CFO CF CF SO F selectivity and CF = CFOCF CF SO CI 100 parts by weight
2 2 2 2 2 2 2 2  2 2 2 2 2 2 2 2
る H O量との関係を示すグラフ。  The graph which shows the relationship with the amount of H 2 O.
2  2
発明を実施するための最良の形態  BEST MODE FOR CARRYING OUT THE INVENTION
[0032] 以下、実施例を挙げて本発明を更に詳細に説明する。 Hereinafter, the present invention will be described in more detail with reference to examples.
[0033] 実施例 1 [0033] Example 1
200mlの 4つ口フラスコに撹拌子、温度計差込管、蛇管式冷却管を取り付け、 CF =  Attach a stirring bar, thermometer plug, and conical tube condenser to a 200 ml four-necked flask, CF =
2 2
CFOCF CF SO C1を 40.0g、 KFを 22.0g及び水を 0.6g (CF =CFOCF CF SO CI 100重CFOCF CF SO C1 40.0g, KF 22.0g and water 0.6g (CF = CFOCF CF SO CI 100
2 2 2 2 2 2 2 量部に対して 1.5重量部)を仕込んだ。撹拌しながら反応器を加熱し、 95 °Cで還流さ せた。反応中、還流温度は低下し 75 °Cで一定となったところで反応を止めた。合計 反応時間は 2時間であった。 2 2 2 2 2 2 2 1.5 parts by weight). The reactor was heated with stirring and refluxed at 95 ° C. During the reaction, the reflux temperature dropped and the reaction was stopped when it became constant at 75 ° C. The total reaction time was 2 hours.
[0034] 反応後、水を加えて白色固体を溶解させ、二層からなる反応溶液を得た。生成物を 二層に液液分離し、得られた有機層をガスクロマトグラフィー内部標準法で定量した ところ、 CF =CFOCF CF SO CI転化率 98. 4%、選択率 99. 3%で、 CF =CFO CF C [0034] After the reaction, water was added to dissolve the white solid to obtain a reaction solution consisting of two layers. The product was liquid-liquid separated into two layers, and the resulting organic layer was quantified by gas chromatography internal standard method. CF = CFOCF CF SO CI conversion 98.4%, selectivity 99.3%, CF = CFO CF C
2 2 2 2 2 2 2 2 2 2 2 2
F SO Fが生成していることが判った。また、得られた水層を19 F NMR内部標準法で定It was found that F SO F was generated. The obtained aqueous layer was determined by 19 F NMR internal standard method.
2 2 twenty two
量したところ、 KF、 KC1の他に CF =CF〇CF CF SO Kが選択率 0.1%、 CF CHFOCF C  As a result, in addition to KF and KC1, CF = CF ○ CF CF SO K has a selectivity of 0.1%, CF CHFOCF C
2 2 2 3 3 2 2 2 2 3 3 2
F SO Fが選択率 0.1%、 CF CHFOCF CF SO Kが選択率 0.5%で生成したことが確認でIt was confirmed that F SO F was produced with a selectivity of 0.1% and CF CHFOCF CF SO K with a selectivity of 0.5%.
2 2 3 2 2 3 2 2 3 2 2 3
きた。  Came.
[0035] 実施例 2〜5及び比較例 1〜4  [0035] Examples 2 to 5 and Comparative Examples 1 to 4
実施例 1と同様の方法で、原料における CF =CFOCF CF SO CIに対する H O量を  In the same manner as in Example 1, the amount of H 2 O with respect to CF = CFOCF CF SO CI in the raw material was determined.
2 2 2 2 2 変化させて、表 1に示す仕込量で CF =CFO CF CF SO Fを合成した。  2 2 2 2 2 By changing, CF = CFO CF CF SO F was synthesized with the charge shown in Table 1.
2 2 2 2  2 2 2 2
[0036] 生成物中の各成分の選択率を表 1に示す。また、 CF =CFOCF CF SO CIに対する  [0036] Table 1 shows the selectivity of each component in the product. Also for CF = CFOCF CF SO CI
2 2 2 2  2 2 2 2
H O量と、 CF =CFOCF CF SO F選択率との関係を図 1に示す。尚、表 1及び図 1で Figure 1 shows the relationship between the amount of H 2 O and CF = CFOCF CF SO F selectivity. In Table 1 and Figure 1,
2 2 2 2 2 2 2 2 2 2
は、 H 0添加量は、 CF =CFOCF CF SO CI 100重量部に対する重量部で表す。  The amount of H 0 added is expressed in parts by weight with respect to 100 parts by weight of CF = CFOCF CF SO CI.
2 2 2 2 2  2 2 2 2 2
[0037] [表 1] 実施例 比較例 [0037] [Table 1] Examples Comparative examples
2 3 4 5 1 2 3 4 仕 H20 (g) 0.04 1.0 3.3 5.4 9.0 20.0 63.6 100 込 CF,=CF0CF2CF2S02C1 (g) 67.2 66.9 66.9 66.9 66.7 66.7 67.6 20 量 KF (結晶品) (g) 36.7 37.0 36.8 37.0 36.7 37.0 37.6 11.72 3 4 5 1 2 3 4 Finish H 2 0 (g) 0.04 1.0 3.3 5.4 9.0 20.0 63.6 100 included CF, = CF0CF 2 CF 2 S0 2 C1 (g) 67.2 66.9 66.9 66.9 66.7 66.7 67.6 20 Quantity KF (Crystalline product) ) ( G ) 36.7 37.0 36.8 37.0 36.7 37.0 37.6 11.7
H20添加量 (重量部) 0.05 1.5 5.0 8.0 13.5 30.0 94.1 500 選 CF2=CF0 CF2CF2S02F 97.8 99.3 99.2 98.5 94.4 91.1 82.8 41.4 択 CF3CHF0CF2CF2S02F 0.5 0.1 0.1 0.2 1.8 2.1 4.4 0.0 率 CF2=CF0CF2CF2S03K 0.3 0.1 0.2 0.4 0.8 2.3 4.7 17.5H 2 0 addition (part by weight) 0.05 1.5 5.0 8.0 13.5 30.0 94.1 500 selection CF 2 = CF0 CF 2 CF 2 S0 2 F 97.8 99.3 99.2 98.5 94.4 91.1 82.8 41.4 selection CF 3 CHF0CF 2 CF 2 S0 2 F 0.5 0.1 0.1 0.2 1.8 2.1 4.4 0.0 Ratio CF 2 = CF0CF 2 CF 2 S0 3 K 0.3 0.1 0.2 0.4 0.8 2.3 4.7 17.5
(%) CF3CHF0CF2CF2S03K 1.4 0.5 0.5 0.9 2.5 4.5 3.2 41.1 以上の結果から、 CF =CFOCF CF SO CI 100重量部に対する H O量が 0. 05〜9 (%) CF 3 CHF0CF 2 CF 2 S0 3 K 1.4 0.5 0.5 0.9 2.5 4.5 3.2 41.1 From the above results, the amount of HO for 100 parts by weight of CF = CFOCF CF SO CI is 0.05 to 9
2 2 2 2 2  2 2 2 2 2
重量部の範囲内の場合に、 CF2=CFO CF2CF2SO Fの選択率力 ¾7%以上となり、顕著 に高 、選択率となることが明らかである。 When it is within the range of parts by weight, the selectivity power of CF 2 = CFO CF 2 CF 2 SO F is ¾7% or more, and it is clear that the selectivity is remarkably high.

Claims

請求の範囲 The scope of the claims
[1] 化学式: CF =CF(CF ) 0(CF CF(CF )0) (CF ) SO Cl(式中、 aは 0又は 1、 bは 0〜5  [1] Chemical formula: CF = CF (CF) 0 (CF CF (CF) 0) (CF) SO Cl (where a is 0 or 1, b is 0 to 5
2 2 a 2 3 b 2 c 2  2 2 a 2 3 b 2 c 2
の整数、 cは 1〜10の整数である)で表される含フッ素クロロスルホ -ルアルキルビ- ルエーテルと化学式: MF-(HF) (式中、 Mはアルカリ金属であり、 Xは 0〜5の整数で ある)で表されるフッ素ィ匕剤とを反応させて、化学式: CF =CF(CF ) 0(CF CF(CF )0)  And a chemical formula: MF- (HF) (wherein M is an alkali metal and X is an integer of 0 to 5) And a chemical formula: CF = CF (CF) 0 (CF CF (CF) 0)
2 2 a 2 3 2 2 a 2 3
(CF ) SO F (式中、 a、 b及び cは上記に同じ)で表される含フッ素フルォロスルホ-ル b 2 c 2 (CF) SO F (wherein a, b and c are the same as above) fluorinated fluorosulfol b 2 c 2
アルキルビュルエーテルを製造する方法であって、原料とする含フッ素クロロスルホ A method for producing an alkyl butyl ether comprising a fluorine-containing chlorosulfo as a raw material
-ルアルキルビュルエーテル 100重量部に対して 0. 05〜9重量部の水の存在下に 反応を行うことを特徴とする方法。 -A method characterized in that the reaction is carried out in the presence of 0.05 to 9 parts by weight of water with respect to 100 parts by weight of rualkylbulle ether.
[2] ィ匕学式: CF =CF(CF ) 0(CF CF(CF )0) (CF ) SO CIにおいて、 a力 0、 b力 0又は 1、 [2] Key equation: CF = CF (CF) 0 (CF CF (CF) 0) (CF) SO CI, a force 0, b force 0 or 1,
2 2 a 2 3 b 2 c 2  2 2 a 2 3 b 2 c 2
cが 1〜4の整数である含フッ素クロロスルホ -ルアルキルビュルエーテルを原料とし て用いる請求項 1に記載の方法。  2. The method according to claim 1, wherein a fluorine-containing chlorosulfoalkyl alkyl ether whose c is an integer of 1 to 4 is used as a raw material.
[3] フッ素化剤力 化学式: MF-(HF)において Mが Kの化合物及び Mが Naの化合物か らなる群力 選ばれた少なくとも一種である請求項 1又は 2に記載の方法。 [3] The method according to claim 1 or 2, wherein the fluorinating power is at least one selected from the group consisting of a compound in which M is K and M is Na in MF- (HF).
[4] 原料とする含フッ素クロロスルホ -ルアルキルビュルエーテル 100重量部に対して 0[4] 0 per 100 parts by weight of fluorine-containing chlorosulfuralkylalkyl ether as raw material
. 1〜6重量部の水の存在下に反応を行う請求項 1〜3のいずれかに記載の方法。 The method according to any one of claims 1 to 3, wherein the reaction is carried out in the presence of 1 to 6 parts by weight of water.
PCT/JP2007/061456 2006-06-07 2007-06-06 Method for producing fluorinated fluorosulfonylalkyl vinyl ether WO2007142266A1 (en)

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JP2003221378A (en) * 2002-01-03 2003-08-05 Ausimont Spa Alkyl ester of 2-(2-fluorosulfonyl)- perfluoroethylenoxy-3-halogen-propionic acid and production method therefor
JP2004244401A (en) * 2002-12-19 2004-09-02 Daikin Ind Ltd Method for producing fluorine-containing fluorosulfonylalykyl vinyl ether
WO2005003082A1 (en) * 2003-07-04 2005-01-13 Asahi Glass Company, Limited Process for production of fluorinated sulfonyl fluorides

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JP2003221378A (en) * 2002-01-03 2003-08-05 Ausimont Spa Alkyl ester of 2-(2-fluorosulfonyl)- perfluoroethylenoxy-3-halogen-propionic acid and production method therefor
JP2004244401A (en) * 2002-12-19 2004-09-02 Daikin Ind Ltd Method for producing fluorine-containing fluorosulfonylalykyl vinyl ether
WO2005003082A1 (en) * 2003-07-04 2005-01-13 Asahi Glass Company, Limited Process for production of fluorinated sulfonyl fluorides

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Publication number Priority date Publication date Assignee Title
JP7565809B2 (en) 2021-01-22 2024-10-11 旭化成株式会社 A method for producing fluorine-containing vinyl sulfonic acid fluoride or a fluorine-containing vinyl sulfonate, and a method for separating the same.

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