WO2005073182A1 - Method for producing fluorine-containing unsaturated sulfonyl fluoride - Google Patents
Method for producing fluorine-containing unsaturated sulfonyl fluoride Download PDFInfo
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- WO2005073182A1 WO2005073182A1 PCT/JP2005/001005 JP2005001005W WO2005073182A1 WO 2005073182 A1 WO2005073182 A1 WO 2005073182A1 JP 2005001005 W JP2005001005 W JP 2005001005W WO 2005073182 A1 WO2005073182 A1 WO 2005073182A1
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- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C303/00—Preparation of esters or amides of sulfuric acids; Preparation of sulfonic acids or of their esters, halides, anhydrides or amides
- C07C303/02—Preparation 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
- C07C303/22—Preparation 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
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- the present invention relates to a method for producing a fluorinated unsaturated sulfonyl fluoride.
- perfluorofluorosulfonylalkyl vinyl ether is a compound useful as an industrial raw material such as an ion exchange membrane material.
- a method for producing perfluorofluorosulfonylalkylbierether a method of reacting perfluorochlorosulfonylalkylvinylether with an alkali metal fluoride is known.
- Patent Document 1 A method of using FCFSOF is known.
- Patent Document 2 In this method, in order to obtain a fluorinated product in high yield, it is necessary to use sulfolane, formamide, or the like as a solvent. Even if it is fluorinated, the yield of CF SO F
- Patent Document 1 US Patent No. 3,560,568
- Patent Document 2 UK Patent No. 1,034,197
- the present invention has been made in view of the above-mentioned state of the art, and the main object of the present invention is to reduce the cost of fluorine-containing sulfonyl fluoride having an unsaturated bond by an industrially advantageous method. Is also to provide a method which can be easily produced with high selectivity and high yield.
- the present inventor has found that when a fluorine-containing sulfonyl chloride having at least one unsaturated bond is used as a raw material, hydrofluoric acid of a specific amine or pyridine compound is used. It has been found that the use of a salt as a fluorinating agent makes it possible to produce a fluorinated sulfonyl fluoride with a high selectivity and a high yield by a simple method. Reached.
- the present invention provides the following method for producing a fluorinated sulfonyl fluoride.
- R SO C1 (where R is a fluorine-containing f 2 f having at least one unsaturated bond)
- R, R and R are the same or different and each represents an alkyl group or a cycloalkyl group
- n is an integer of 1 to 9
- R, R and R are the same or different and are a hydrogen atom or an alkyl group, and n is 1
- R and R are the same or different and are each a hydrogen atom or an alkyl group, and n is 1
- d e is an integer of 9 and m is an integer of 2 or more).
- X is 0, S or NH
- R is a group which may have a fluorine atom as a substituent.
- the fluorinating agent has the chemical formula: [0015] [Formula 4]
- R, R and R are the same or different and are a lower alkyl group, and n is 3)
- a fluorine-containing unsaturated sulfonyl chloride represented by a chemical formula: RSOC1 is used as a raw material.
- R is a fluorinated hydrocarbon having at least one unsaturated bond f
- the fluorine-containing hydrocarbon group may contain at least one element selected from oxygen, nitrogen and zeolite.
- the unsaturated bond may be a double bond or a triple bond, and both may be contained simultaneously.
- the position of the unsaturated bond is not limited. Further, in the fluorinated hydrocarbon group, all hydrogen atoms may be substituted by fluorine atoms, or only some hydrogen atoms may be substituted.
- the fluorine-containing hydrocarbon group represented by R includes the following formula:
- X is ⁇ , S or NH
- R is a divalent hydrocarbon group which may have a fluorine atom as a substituent
- p is an integer of 0-4.
- R include a linear or branched alkylene group, an arylene group, and g
- Examples thereof include a divalent hydrocarbon group such as a group to which these are bonded.
- the hydrocarbon group may further contain at least one element selected from oxygen, zeolite and nitrogen.
- Examples of the alkylene group include groups having about 118 carbon atoms.
- Examples of the arylene group include a phenylene group. These divalent hydrocarbon groups are In addition, some or all of the hydrogen atoms may be substituted or unsubstituted.
- fluorine-containing hydrocarbon group represented by R include the following formula:
- q is an integer of 0-3.
- the fluorine-containing unsaturated sulfo-urquose is reacted with at least one kind of fluorinating agent selected from the compounds described in the following (i)-(iii) to obtain a fluorine-containing unsaturated sulfo-yoke.
- a saturated sulfonyl fluoride can be obtained.
- R, R and R are the same or different and each represents an alkyl group or a cycloalkyl group
- n is an integer of 1 to 9
- R, R and R are the same or different and are a hydrogen atom or an alkyl group, and n is 1
- R and R are the same or different and are each a hydrogen atom or an alkyl group, and n is
- n is an integer of 2 or more).
- R is the same or different.
- the alkyl group include straight-chain or branched-chain alkyl groups having about 119 carbon atoms, such as methyl, ethyl, isopropyl, n-propyl, n-butyl, t-butyl, sec-butyl and the like.
- a lower alkyl group having about 114 carbon atoms is preferable.
- Examples of the cycloalkyl group include groups having about 5 to 8 carbon atoms, such as cyclopentyl, cyclohexyl, and cyclooctyl.
- n is an integer from 1 to 9, preferably an integer from 2 to 9.
- a and R are the same or different b c
- a hydrogen atom or an alkyl group examples include the same groups as the alkyl groups of the alkylamine hydrofluoride described in (i) above.
- n is an integer of 1 to 9, preferably an integer of 2 to 9.
- n is an integer of 1 to 9, preferably an integer of 2 to 9.
- m is an integer of 2 or more, and the weight average molecular weight is in the range of about 4 000 to 160,000.
- the fluorinating agent comprising the compound described in the above (i) item (iii) can be used alone or in combination of two or more. By using these fluorinating agents, the desired fluorinated unsaturated sulfonyl fluoride can be obtained with high selectivity and high yield.
- the fluorinated salt is used as the fluorinating agent
- the desired fluorine-containing unsaturated sulfonyl fluoride can be obtained with a high conversion and a high selectivity, and the handling can be easily performed.
- the method of reacting the fluorinated unsaturated sulfourukulide used as a raw material with a fluorinating agent is not particularly limited, and both may be charged at the same time and reacted, or either one of the raw material and the fluorinating agent The other may be dropped.
- a method of dropping one of the raw material and the fluorinating agent with the other is advantageous in that the accumulation of reaction heat can be prevented.
- the amount of the fluorinating agent to be used is preferably about 0.1 to 10 mol, and more preferably about 115 mol, per mol of the fluorinated unsaturated sulfo-uricide used as a raw material. .
- the fluorinating agent is used in an amount of about 2 to 3 moles per mole of the fluorinated unsaturated sulfo-mouth compound, the desired product can be obtained at a high conversion rate.
- the number of moles of the polyvinylpyridine hydrofluoride described in the above (m) is a structural unit represented by the following formula.
- the reaction can be carried out without a solvent or in a solvent, but is preferably carried out without a solvent in terms of cost.
- a solvent a polar solvent or a non-polar solvent that does not participate in the reaction can be used. Specific examples include CH CI, CHC1, CH CN, N, N-dimethylformamide (DMF)
- the amount may be, for example, about 115 parts by weight with respect to 100 parts by weight of the fluorine-containing unsaturated sulfo-mouth compound.
- the reaction temperature is preferably about -20 ° C to about 100 ° C, and more preferably about 10 ° C to about 40 ° C.
- the reaction time is generally about 0.01 hour to 48 hours, preferably about 0.5 to 24 hours.
- the reaction pressure may be any of reduced pressure, atmospheric pressure, and increased pressure, but it is preferable to carry out the reaction under atmospheric pressure.
- the obtained crude product is usually separated into three phases.
- the upper phase is the fluorinating agent
- the lower phase is the desired fluorinated unsaturated sulfonyl fluoride phase
- the middle phase is the hydrofluoric acid salt of the fluorinating agent, for example, when alkylamine hydrofluoride is used as the fluorinating agent.
- alkylamine hydrochloride or pyridin hydrofluoride is used as a fluorinating agent
- pyridine hydrochloride is used
- polybutylpyridine hydrofluoride is used as a fluorinating agent
- polybutylpyridine hydrochloride polybutylpyridine hydrochloride is used.
- the desired fluorinated unsaturated sulfonyl fluoride can be purified by a known method such as filtration, distillation, column chromatography and the like.
- a known method such as filtration, distillation, column chromatography and the like.
- perfluoroalkylvinylsulfonyl fluoride is a substance useful as a monomer component for an electrolyte polymer.
- anhydrous HF is added to the remaining two-phase mixture of the fluorinating agent and the hydrochloride of the fluorinating agent.
- the hydrochloride of the fluorinating agent can be converted to hydrofluoric acid and regenerated as the fluorinating agent.
- the amount of anhydrous HF used may be about 0.1 to 100 moles per mol of the hydrochloride of the fluorinating agent. It is preferred to use a molar excess of anhydrous HF.
- the reaction temperature is preferably in the range of about -20 ° C to about 100 ° C, and is preferably in the range of about 0 ° C to about 40 ° C.
- the reaction time is preferably about 0.01 to 48 hours, and preferably about 0.5 to 24 hours.
- the reaction pressure may be any of reduced pressure, atmospheric pressure, and pressurized pressure, but it is preferable to carry out the reaction under atmospheric pressure or pressurized pressure up to about 5.0 MPa (gauge pressure).
- the hydrochloride of the fluorinating agent can be converted to hydrofluoric acid and regenerated as the fluorinating agent.
- the fluorinating agent used in the present invention can be regenerated and recycled by a simple method. Therefore, the method of the present invention can be said to be a production method with a low environmental load capable of reducing industrial waste.
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Abstract
Description
明 細 書 Specification
含フッ素不飽和スルホニルフロライドの製造方法 Process for producing fluorine-containing unsaturated sulfonyl fluoride
技術分野 Technical field
[0001] 本発明は、含フッ素不飽和スルホニルフロライドの製造方法に関する。 The present invention relates to a method for producing a fluorinated unsaturated sulfonyl fluoride.
背景技術 Background art
[0002] 不飽和結合を有する含フッ素スルホニルフロライドの内で、例えば、パーフルオロフ ルォロスルホニルアルキルビニルエーテルは、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。 [0002] Among fluorine-containing sulfonyl fluorides having an unsaturated bond, for example, perfluorofluorosulfonylalkyl vinyl ether is a compound useful as an industrial raw material such as an ion exchange membrane material.
[0003] パーフルオロフルォロスルホニルアルキルビエルエーテルの製造方法としては、パ 一フルォロクロロスルホニルアルキルビニルエーテルとアルカリ金属フッ化物とを反応 させる方法が知られている。例えば、フッ素化剤として NaFを用レ、、スルホラン溶媒中 で、 CF =CFOCF CF SO CIで表される化合物を NaFと反応させて CF =CFOC [0003] As a method for producing perfluorofluorosulfonylalkylbierether, a method of reacting perfluorochlorosulfonylalkylvinylether with an alkali metal fluoride is known. For example, using NaF as a fluorinating agent, CF = CFOCF CF SO CI in a sulfolane solvent is reacted with NaF to obtain CF = CFOC
2 2 2 2 2 2 2 2 2 2
F CF SO Fとする方法が知られている(特許文献 1)。 A method of using FCFSOF is known (Patent Document 1).
2 2 2 2 2 2
[0004] し力しながら、この方法では、十分に高い選択率で目的とするスルホニルフロライド を得ることができない。更に、溶媒として低融点、高沸点を有するスルホランを用いる ために、未反応原料の NaF、副生成物である NaCl等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、 工業的実施が困難であり、産業廃棄物が多量に生じるという問題もある。 [0004] However, with this method, the desired sulfonyl fluoride cannot be obtained with a sufficiently high selectivity. Furthermore, since sulfolane having a low melting point and a high boiling point is used as a solvent, it is difficult to separate unreacted raw materials such as NaF and by-products such as NaCl. It becomes very complicated. Therefore, this method has a problem that it is difficult to implement industrially and a large amount of industrial waste is generated.
[0005] パーフルォロアルキル基を有する化合物、例えば、 C F SO C1を原料とする場合 When a compound having a perfluoroalkyl group, for example, C F SO C1 is used as a raw material
8 17 2 8 17 2
には、 KFを用いてフッ素化することにより C F SO Fが得られることが報告されてい Reports that fluorination with KF can provide C F SO F
8 17 2 8 17 2
る(特許文献 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 (Patent Document 2). In this method, in order to obtain a fluorinated product in high yield, it is necessary to use sulfolane, formamide, or the like as a solvent. Even if it is fluorinated, the yield of CF SO F
8 17 2 8 17 2
ぎず、工業的実施には不適切である。 Inadequate for industrial implementation.
特許文献 1:米国特許第 3,560,568号 Patent Document 1: US Patent No. 3,560,568
特許文献 2:英国特許第 1,034,197号 Patent Document 2: UK Patent No. 1,034,197
発明の開示 発明が解決しょうとする課題 Disclosure of the invention Problems the invention is trying to solve
[0006] 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 、不飽和結合を有する含フッ素スルホニルフロライドを工業的に有利な方法で、安価 にし力、も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。 [0006] The present invention has been made in view of the above-mentioned state of the art, and the main object of the present invention is to reduce the cost of fluorine-containing sulfonyl fluoride having an unsaturated bond by an industrially advantageous method. Is also to provide a method which can be easily produced with high selectivity and high yield.
課題を解決するための手段 Means for solving the problem
[0007] 本発明者は、上記した目的を達成すべく鋭意研究を重ねた結果、少なくとも一個の 不飽和結合を有する含フッ素スルホニルクロライドを原料とする場合に、特定のァミン 又はピリジン化合物のフッ酸塩をフッ素化剤として用いることにより、簡便な方法によ つて、高い選択率で、収率よく含フッ素スルホニルフロライドを製造することが可能と なることを見出し、ここに本発明を完成するに至った。 As a result of intensive studies to achieve the above object, the present inventor has found that when a fluorine-containing sulfonyl chloride having at least one unsaturated bond is used as a raw material, hydrofluoric acid of a specific amine or pyridine compound is used. It has been found that the use of a salt as a fluorinating agent makes it possible to produce a fluorinated sulfonyl fluoride with a high selectivity and a high yield by a simple method. Reached.
[0008] 即ち、本発明は、下記の含フッ素スルホニルフロライドの製造方法を提供するもの である。 [0008] That is, the present invention provides the following method for producing a fluorinated sulfonyl fluoride.
1. 化学式: R SO C1 (式中、 Rは、少なくとも一個の不飽和結合を有する含フッ素 f 2 f 1. Chemical formula: R SO C1 (where R is a fluorine-containing f 2 f having at least one unsaturated bond)
炭化水素基であり、該含フッ素炭化水素基には、酸素、窒素及びィォゥから選ばれ た少なくとも一個の元素が含まれていてもよレ、)で表される含フッ素不飽和スルホ二 ルクロライドを、下記 )一 (m)項に示す化合物から選ばれた少なくとも一種のフッ素 化剤と反応させることを特徴とする化学式: R S〇 F (式中、 Rは、上記に同じ)で表さ f 2 f A fluorine-containing unsaturated sulfonyl chloride represented by the formula: wherein the fluorine-containing hydrocarbon group may contain at least one element selected from oxygen, nitrogen and iodide. Is reacted with at least one kind of fluorinating agent selected from the following compounds (1) (m): RS〇F (where R is the same as above). 2 f
れる含フッ素不飽和スルホニルフロライドの製造方法: For producing the fluorine-containing unsaturated sulfonyl fluoride to be used:
(i)化学式: (i) Chemical formula:
[0009] [化 1] [0009] [Formula 1]
[0010] (式中、 R、 R及び Rは、同一又は異なって、アルキル基又はシクロアルキル基であ (Wherein, R, R and R are the same or different and each represents an alkyl group or a cycloalkyl group
1 2 3 one two Three
り、 nは 1一 9の整数である)で表されるアルキルアミンフッ酸塩、 Wherein n is an integer of 1 to 9),
(ii)化学式: (ii) Chemical formula:
[0012] (式中、 R、 R及び Rは、同一又は異なって水素原子又はアルキル基であり、 nは 1 (Wherein, R, R and R are the same or different and are a hydrogen atom or an alkyl group, and n is 1
a b c a b c
一 9の整数である)で表されるピリジンフッ酸塩、 A pyridine hydrochloride represented by the formula:
(iii)化学式: (iii) Chemical formula:
[0013] [化 3] [0013] [Formula 3]
[0014] (式中、 R及び Rは、同一又は異なって、水素原子又はアルキル基であり、 nは 1 (Wherein, R and R are the same or different and are each a hydrogen atom or an alkyl group, and n is 1
d e 一 9 の整数、 mは 2以上の整数である)で表されるポリビュルピリジンフッ酸塩。 d e is an integer of 9 and m is an integer of 2 or more).
2. 化学式: R SO C1において、 Rが、 2. Chemical formula: In RSO C1, R is
f 2 f f 2 f
式: CF =CF- (CF ) -X-R - Formula: CF = CF- (CF) -X-R-
2 2 p g 2 2 p g
(式中、 Xは、 0、 S又は NHであり、 Rは、置換基としてフッ素原子を有することのある g (In the formula, X is 0, S or NH, and R is a group which may have a fluorine atom as a substituent.
二価の炭化水素基であり、 Pは、 0— 4の整数である)で表される基である上記項 1に 記載の方法。 2. The method according to the above item 1, wherein the group is a divalent hydrocarbon group, and P is an integer of 0-4.
3. 化学式: R SO C1において、 Rが、 3. Chemical formula: In RSO C1, R is
f 2 f f 2 f
式: CF =CF-〇一 [CF CF (CF ) 0] CF CF - Formula: CF = CF-〇 一 [CF CF (CF) 0] CF CF-
2 2 3 q 2 2 2 2 3 q 2 2
(式中、 qは 0— 3の整数である。)で表される基である上記項 2に記載の方法。 (Where q is an integer of 0-3). The method according to the above item 2, which is a group represented by the formula:
4. フッ素化剤が、化学式: [0015] [化 4] 4. The fluorinating agent has the chemical formula: [0015] [Formula 4]
R— N ' (HF)n R— N '(HF) n
[0016] (式中、 R、 R及び Rは、同一又は異なって、低級アルキル基であり、 nは 3である) (Wherein, R, R and R are the same or different and are a lower alkyl group, and n is 3)
1 2 3 one two Three
で表されるアルキルアミンフッ酸塩である上記項 1一 3のいずれかに記載の方法。 5. 上記項 1一 4のいずれかの方法によって含フッ素不飽和スルホニルフロライドを 製造した後、反応粗生成物から該含フッ素不飽和スルホニルフロライドを分離し、次 レ、で、残留するフッ素化剤の塩酸塩を無水 HFと反応させてフッ酸塩に変換すること を特徴とするフッ素化剤の再生方法。 14. The method according to any one of the above items 13 to 13, which is an alkylamine hydrochloride represented by the formula: 5. After producing the fluorinated unsaturated sulfonyl fluoride by any one of the above-mentioned items 1-4, the fluorinated unsaturated sulfonyl fluoride is separated from the crude reaction product, and the remaining fluorine is removed in the next step. A method for regenerating a fluorinating agent, comprising reacting the hydrochloride of the agent with anhydrous HF to convert it to hydrofluoric acid.
[0017] 本発明の含フッ素不飽和スルホニルフロライドの製造方法では、原料としては、化 学式: R SO C1で表される含フッ素不飽和スルホニルクロライドを用いる。 In the method for producing a fluorine-containing unsaturated sulfonyl chloride of the present invention, a fluorine-containing unsaturated sulfonyl chloride represented by a chemical formula: RSOC1 is used as a raw material.
f 2 f 2
[0018] 上記化学式において、 Rは、少なくとも一個の不飽和結合を有する含フッ素炭化水 f In the above chemical formula, R is a fluorinated hydrocarbon having at least one unsaturated bond f
素基であり、該含フッ素炭化水素基には、酸素、窒素及びィォゥから選ばれた少なく とも一個の元素が含まれていても良い。不飽和結合は、二重結合、三重結合の何れ でもよく、両者が同時に含まれていても良い。不飽和結合の位置についても限定は なレ、。また、含フッ素炭化水素基では、フッ素原子によって全ての水素原子が置換さ れてレ、てもよく、或いは一部の水素原子のみが置換されてレ、ても良レ、。 And the fluorine-containing hydrocarbon group may contain at least one element selected from oxygen, nitrogen and zeolite. The unsaturated bond may be a double bond or a triple bond, and both may be contained simultaneously. The position of the unsaturated bond is not limited. Further, in the fluorinated hydrocarbon group, all hydrogen atoms may be substituted by fluorine atoms, or only some hydrogen atoms may be substituted.
[0019] Rで表される含フッ素炭化水素基としては、下記式: The fluorine-containing hydrocarbon group represented by R includes the following formula:
f f
CF =CF— (CF ) -X-R - CF = CF— (CF) -X-R-
2 2 p g 2 2 p g
で表される基を例示できる。上記式において、 Xは、〇、 S又は NHであり、 Rは、置 換基としてフッ素原子を有することのある二価の炭化水素基であり、 pは 0— 4の整数 である。 Can be exemplified. In the above formula, X is 〇, S or NH, R is a divalent hydrocarbon group which may have a fluorine atom as a substituent, and p is an integer of 0-4.
[0020] Rの具体例としては、直鎖状若しくは分枝鎖状のアルキレン基、ァリーレン基又は g [0020] Specific examples of R include a linear or branched alkylene group, an arylene group, and g
これらが結合した基などの二価の炭化水素基を挙げることができる。該炭化水素基に は、更に、酸素、ィォゥ及び窒素から選ばれた少なくとも一種の元素が含まれていて もよレ、。アルキレン基としては、炭素数 1一 8程度の基を例示できる。ァリーレン基とし ては、フエ二レン基等を例示できる。これらの二価の炭化水素基は、フッ素原子によ つて一部又は全ての水素原子が置換されていてもよぐ或いは未置換であっても良 レ、。 Examples thereof include a divalent hydrocarbon group such as a group to which these are bonded. The hydrocarbon group may further contain at least one element selected from oxygen, zeolite and nitrogen. Examples of the alkylene group include groups having about 118 carbon atoms. Examples of the arylene group include a phenylene group. These divalent hydrocarbon groups are In addition, some or all of the hydrogen atoms may be substituted or unsubstituted.
[0021] Rで表される含フッ素炭化水素基の具体例としては、下記式: [0021] Specific examples of the fluorine-containing hydrocarbon group represented by R include the following formula:
f f
CF =CF—〇一 [CF CF (CF )〇] CF CF - CF = CF—〇 一 [CF CF (CF) 〇] CF CF-
2 2 3 q 2 2 2 2 3 q 2 2
で表される基を挙げることができる。上記式において、 qは 0— 3の整数である。 And the group represented by In the above formula, q is an integer of 0-3.
[0022] 本発明によれば、上記した含フッ素不飽和スルホユルク口ライドを下記(i)一 (iii)項 に記載した化合物から選ばれる少なくとも一種のフッ素化剤と反応させることによって 、含フッ素不飽和スルホニルフロライドを得ることができる。 [0022] According to the present invention, the fluorine-containing unsaturated sulfo-urquose is reacted with at least one kind of fluorinating agent selected from the compounds described in the following (i)-(iii) to obtain a fluorine-containing unsaturated sulfo-yoke. A saturated sulfonyl fluoride can be obtained.
(i)化学式: (i) Chemical formula:
[0023] [化 5] [0023] [Formula 5]
R -N - (HF)n R -N-(HF) n
R3 R 3
[0024] (式中、 R、 R及び Rは、同一又は異なって、アルキル基又はシクロアルキル基であ (Wherein, R, R and R are the same or different and each represents an alkyl group or a cycloalkyl group
1 2 3 one two Three
り、 nは 1一 9の整数である)で表されるアルキルアミンフッ酸塩、 Wherein n is an integer of 1 to 9),
(ii)化学式: (ii) Chemical formula:
[0025] [化 6] [0025]
(式中、 R、 R及び Rは、同一又は異なって水素原子又はアルキル基であり、 nは 1 (Wherein, R, R and R are the same or different and are a hydrogen atom or an alkyl group, and n is 1
a b c a b c
一 9の整数である)で表されるピリジンフッ酸塩、 A pyridine hydrochloride represented by the formula:
(iii)化学式: [0027] [化 7] (iii) Chemical formula: [0027] [Formula 7]
[0028] (式中、 R及び Rは、同一又は異なって、水素原子又はアルキル基であり、 nは 1一 9 d e (Wherein, R and R are the same or different and are each a hydrogen atom or an alkyl group, and n is
の整数、 mは 2以上の整数である)で表されるポリビュルピリジンフッ酸塩。 And m is an integer of 2 or more).
[0029] 上記(i)項に記載したアルキルアミンフッ酸塩では、 R 同一又は異 [0029] In the alkylamine hydrofluoride described in the above (i), R is the same or different.
1、 R及び Rは、 1, R and R are
2 3 twenty three
なって、アルキル基又はシクロアルキル基である。アルキル基としては炭素数 1一 9程 度の直鎖状又は分枝鎖状アルキル基を例示でき、特に、メチル、ェチル、イソプロピ ノレ、 n—プロピル、 n—ブチル、 tーブチル、 sec—ブチル等の炭素数 1一 4程度の低級ァ ルキル基が好ましい。シクロアルキル基としては、シクロペンチル、シクロへキシル、シ クロォクチル等の炭素数 5— 8程度の基を例示できる。 nは、 1一 9の整数であり、好ま しくは 2— 9の整数である。 Is an alkyl group or a cycloalkyl group. Examples of the alkyl group include straight-chain or branched-chain alkyl groups having about 119 carbon atoms, such as methyl, ethyl, isopropyl, n-propyl, n-butyl, t-butyl, sec-butyl and the like. A lower alkyl group having about 114 carbon atoms is preferable. Examples of the cycloalkyl group include groups having about 5 to 8 carbon atoms, such as cyclopentyl, cyclohexyl, and cyclooctyl. n is an integer from 1 to 9, preferably an integer from 2 to 9.
[0030] 上記(ii)項に記載したピリジンフッ酸塩において、 R R及び [0030] In the pyridine hydrochloride described in the above (ii), R R and
a、 Rは、同一又は異な b c a and R are the same or different b c
つて水素原子又はアルキル基である。アルキル基としては、上記(i)に記載したアル キルアミンフッ酸塩のアルキル基と同様の基を例示できる。 nは、 1一 9の整数であり、 好ましくは 2— 9の整数である。 A hydrogen atom or an alkyl group. Examples of the alkyl group include the same groups as the alkyl groups of the alkylamine hydrofluoride described in (i) above. n is an integer of 1 to 9, preferably an integer of 2 to 9.
[0031] 上記(iii)項に記載したポリビュルピリジンフッ酸塩にぉレ、て、 R及び Rは、同一又 d e [0031] In the polybutylpyridine hydrofluoride described in the above (iii), R and R are the same or de
は異なって、水素原子又はアルキル基である。ァノレキノレ基としては、上記(i)に記載 したアルキルアミンフッ酸塩のアルキル基と同様の基を例示できる。 nは 1一 9の整数 であり、好ましくは 2— 9の整数である。 mは 2以上の整数であり、重量平均分子量は 4 000— 160000程度の範囲であること力 S好ましレ、。 Is differently a hydrogen atom or an alkyl group. Examples of the phenol group include the same groups as the alkyl groups of the alkylamine hydrofluoride described in (i) above. n is an integer of 1 to 9, preferably an integer of 2 to 9. m is an integer of 2 or more, and the weight average molecular weight is in the range of about 4 000 to 160,000.
[0032] 上記 (i)一 (iii)項に記載した化合物からなるフッ素化剤は、一種単独又は二種以上 混合して用いることができる。これらのフッ素化剤を用いることにより、高い選択率で 収率よく目的とする含フッ素不飽和スルホニルフロライドを得ることができる。 [0032] The fluorinating agent comprising the compound described in the above (i) item (iii) can be used alone or in combination of two or more. By using these fluorinating agents, the desired fluorinated unsaturated sulfonyl fluoride can be obtained with high selectivity and high yield.
[0033] 上記したフッ素化剤の内で、 (i)項に記載したアルキルアミンフッ酸塩については、 nが 2— 9の場合に液状の化合物であるために取り扱いが容易であり、特に、 R [0033] Among the above fluorinating agents, regarding the alkylamine hydrofluoride described in the item (i), When n is 2—9, the compound is a liquid compound and is easy to handle.
1、 R 1, R
2 及び R 1 炭素数 1一 4程度の低級アルキル基であって、 n= 3のアルキルアミン 3フ 2 and R 1 are lower alkyl groups having about 14 carbon atoms and n = 3 alkylamine
3 Three
ッ酸塩をフッ素化剤とする場合には、高い転換率と高い選択率で目的とする含フッ素 不飽和スルホニルフロライドを得ることができ、し力 取り扱レ、も容易である。 When the fluorinated salt is used as the fluorinating agent, the desired fluorine-containing unsaturated sulfonyl fluoride can be obtained with a high conversion and a high selectivity, and the handling can be easily performed.
[0034] 原料として用いる含フッ素不飽和スルホユルク口ライドとフッ素化剤とを反応させる 方法については、特に限定はなぐ両者を同時に仕込んで反応させてもよぐ或いは 原料及びフッ素化剤のいずれか一方に他方を滴下してもよい。特に、原料及びフッ 素化剤のいずれか一方に他方を滴下する方法は、反応熱の蓄積を防ぐことができる 点で有利である。 [0034] The method of reacting the fluorinated unsaturated sulfourukulide used as a raw material with a fluorinating agent is not particularly limited, and both may be charged at the same time and reacted, or either one of the raw material and the fluorinating agent The other may be dropped. In particular, a method of dropping one of the raw material and the fluorinating agent with the other is advantageous in that the accumulation of reaction heat can be prevented.
[0035] フッ素化剤の使用量は、原料として用いる含フッ素不飽和スルホユルク口ライド 1モ ルに対して、 0. 1— 10モル程度とすればよぐ 1一 5モル程度とすることが好ましい。 特に、含フッ素不飽和スルホユルク口ライド 1モルに対してフッ素化剤を 2— 3モル程 度用いる場合には、高い転換率で目的物を得ること力 Sできる。 [0035] The amount of the fluorinating agent to be used is preferably about 0.1 to 10 mol, and more preferably about 115 mol, per mol of the fluorinated unsaturated sulfo-uricide used as a raw material. . In particular, when the fluorinating agent is used in an amount of about 2 to 3 moles per mole of the fluorinated unsaturated sulfo-mouth compound, the desired product can be obtained at a high conversion rate.
[0036] 尚、上記(m)項に記載したポリビニルピリジンフッ酸塩のモル数にっレ、ては、下記 式で表される構成単位 [0036] The number of moles of the polyvinylpyridine hydrofluoride described in the above (m) is a structural unit represented by the following formula.
[0037] [化 8] [0037] [Formula 8]
[0038] の 1個をビエルピリジンフッ酸 1分子として換算したモル数である。 [0038] This is the number of moles when one of the above was converted to one molecule of bierpyridine hydrofluoric acid.
[0039] 反応は無溶媒又は溶媒中で行うことができるが、コスト面からは無溶媒で行うことが 好ましい。溶媒としては、反応に関与しない極性溶媒又は無極性溶媒を用いることが できる。具体例として、 CH CI、 CHC1、 CH CN、 N, N—ジメチルホルムアミド(DMF) The reaction can be carried out without a solvent or in a solvent, but is preferably carried out without a solvent in terms of cost. As the solvent, a polar solvent or a non-polar solvent that does not participate in the reaction can be used. Specific examples include CH CI, CHC1, CH CN, N, N-dimethylformamide (DMF)
2 2 3 3 2 2 3 3
、ジメチルスルホキシド(DMSO)、 H〇、 C F 等を挙げることができる。溶媒の使用量 , Dimethylsulfoxide (DMSO), H〇, C F and the like. Solvent usage
2 6 14 2 6 14
は、例えば、含フッ素不飽和スルホユルク口ライド 100重量部に対して 1一 50重量部 程度とすればよい。 [0040] 反応温度は、 _20°C— 100°C程度とすればよぐ 10°C— 40°C程度とすることが好 ましい。反応時間は、通常、 0. 01時間一 48時間程度であり、好ましくは 0. 5— 24時 間程度である。 The amount may be, for example, about 115 parts by weight with respect to 100 parts by weight of the fluorine-containing unsaturated sulfo-mouth compound. [0040] The reaction temperature is preferably about -20 ° C to about 100 ° C, and more preferably about 10 ° C to about 40 ° C. The reaction time is generally about 0.01 hour to 48 hours, preferably about 0.5 to 24 hours.
[0041] 反応圧力は、減圧、大気圧、加圧のいずれでもよいが、大気圧下で反応を行うこと が好ましい。 [0041] The reaction pressure may be any of reduced pressure, atmospheric pressure, and increased pressure, but it is preferable to carry out the reaction under atmospheric pressure.
[0042] 以上の方法によって、 目的とする含フッ素スルホニルフロライドを高い選択率で製 造すること力 Sできる。 [0042] According to the above method, it is possible to produce the desired fluorine-containing sulfonyl fluoride with high selectivity.
[0043] 得られた粗生成物は、通常、三相に分離する。上相はフッ素化剤、下相は目的とす る含フッ素不飽和スルホニルフロライド相となり、中相はフッ素化剤の塩酸塩、例えば 、アルキルアミンフッ酸塩をフッ素化剤とする場合にはアルキルアミン塩酸塩、ピリジ ンフッ酸塩をフッ素化剤とする場合にはピリジン塩酸塩、ポリビュルピリジンフッ酸塩 をフッ素化剤とする場合には、ポリビュルピリジン塩酸塩となる。 [0043] The obtained crude product is usually separated into three phases. The upper phase is the fluorinating agent, the lower phase is the desired fluorinated unsaturated sulfonyl fluoride phase, and the middle phase is the hydrofluoric acid salt of the fluorinating agent, for example, when alkylamine hydrofluoride is used as the fluorinating agent. When alkylamine hydrochloride or pyridin hydrofluoride is used as a fluorinating agent, pyridine hydrochloride is used, and when polybutylpyridine hydrofluoride is used as a fluorinating agent, polybutylpyridine hydrochloride is used.
[0044] 目的とする含フッ素不飽和スルホニルフロライドは、濾過、蒸留、カラムクロマトダラ フィ一などの公知の方法で精製できる。この様にして得られる含フッ素不飽和スルホ ニルフロライドの内で、例えば、パーフルォロアルキルビニルスルホニルフロライドは 、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。 [0044] The desired fluorinated unsaturated sulfonyl fluoride can be purified by a known method such as filtration, distillation, column chromatography and the like. Among the fluorinated unsaturated sulfonyl fluorides thus obtained, for example, perfluoroalkylvinylsulfonyl fluoride is a substance useful as a monomer component for an electrolyte polymer.
[0045] また、上記した方法で含フッ素不飽和スルホニルフロライドを製造し、回収した後、 残留するフッ素化剤とフッ素化剤の塩酸塩の二相からなる混合物中に、無水 HFを 添加することによって、フッ素化剤の塩酸塩をフッ酸塩に変換して、フッ素化剤として 再生することができる。 Further, after producing and recovering the fluorinated unsaturated sulfonyl fluoride by the method described above, anhydrous HF is added to the remaining two-phase mixture of the fluorinating agent and the hydrochloride of the fluorinating agent. As a result, the hydrochloride of the fluorinating agent can be converted to hydrofluoric acid and regenerated as the fluorinating agent.
[0046] この場合、無水 HFの使用量については、フッ素化剤の塩酸塩に対して 0. 1— 100 倍モル程度とすればよぐ特に、フッ素化剤の塩酸塩に対して 3 20倍モル程度とい う過剰量の無水 HFを使用することが好ましい。 In this case, the amount of anhydrous HF used may be about 0.1 to 100 moles per mol of the hydrochloride of the fluorinating agent. It is preferred to use a molar excess of anhydrous HF.
[0047] 反応温度は、 _20°C— 100°C程度の範囲とすればよぐ 0°C 40°C程度の範囲と することが好ましい。反応時間は、 0. 01 48時間程度とすればよぐ 0. 5— 24時間 程度とすることが好ましい。 [0047] The reaction temperature is preferably in the range of about -20 ° C to about 100 ° C, and is preferably in the range of about 0 ° C to about 40 ° C. The reaction time is preferably about 0.01 to 48 hours, and preferably about 0.5 to 24 hours.
[0048] 反応圧力は、減圧、大気圧、加圧のいずれでもよいが、大気圧下又は 5. 0MPa ( ゲージ圧)程度までの加圧下で反応を行うことが好ましい。 [0049] 以上の方法によって、フッ素化剤の塩酸塩をフッ酸塩に変換して、フッ素化剤とし て再生することができる。 [0048] The reaction pressure may be any of reduced pressure, atmospheric pressure, and pressurized pressure, but it is preferable to carry out the reaction under atmospheric pressure or pressurized pressure up to about 5.0 MPa (gauge pressure). [0049] By the above method, the hydrochloride of the fluorinating agent can be converted to hydrofluoric acid and regenerated as the fluorinating agent.
[0050] 特に、式:(CH ) Ν· (HF) nにおいて、 nが 2· 5— 3· 5程度のフッ酸塩については [0050] In particular, in the formula: (CH 2) Ν · (HF) n, for a hydrofluoric acid salt in which n is about 2.5
3 3 3 3
、蒸留によって簡単に分離できるので、簡単な方法で純度のよいフッ素化剤として再 生できる。 Since it can be easily separated by distillation, it can be regenerated as a highly pure fluorinating agent by a simple method.
発明の効果 The invention's effect
[0051] 本発明方法によれば、煩雑な操作を要することなぐ工業的に有利な方法によって 、 目的とする含フッ素不飽和スルホニルフロライドを高い選択率で収率良く製造する こと力 Sできる。 According to the method of the present invention, it is possible to produce the desired fluorinated unsaturated sulfonyl fluoride with high selectivity and high yield by an industrially advantageous method that does not require complicated operations.
[0052] また、本発明で用いるフッ素化剤は、簡単な方法で再生してリサイクルすることがで きる。従って、本発明方法は、産業廃棄物を低減することが可能な環境負荷の低い 製造方法といえる。 [0052] The fluorinating agent used in the present invention can be regenerated and recycled by a simple method. Therefore, the method of the present invention can be said to be a production method with a low environmental load capable of reducing industrial waste.
発明を実施するための最良の形態 BEST MODE FOR CARRYING OUT THE INVENTION
[0053] 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.
[0054] 実施例 1 Example 1
CF =CFOCF CF SO Fの製诰 CF = CFOCF CF SO F
2 2 2 2 2 2 2 2
ジムロート及び滴下ロートを取り付けた 100ml三つ口フラスコを用意し、このフラスコ にトリエチルァミン 3フッ酸塩(Et N : (HF) )を 33. 5g(208. Immol)仕込み、滴下 Prepare a 100 ml three-necked flask equipped with a dim funnel and a dropping funnel, and add 33.5 g (208. Immol) of triethylamine trifluoride (Et N: (HF)) to the flask, and add dropwise.
3 3 3 3
ロートに CF =CFOCF CF SO CIを 20. 0g (67. 5mmol)仕込んだ(仕込みモル The funnel was charged with 20.0 g (67.5 mmol) of CF = CFOCF CF SO CI (the charged mole).
2 2 2 2 2 2 2 2
比 3:1)。 Ratio 3: 1).
[0055] 室温下 (22°C)で攪拌を行ないながら、 CF =CFOCF CF SO CIを 1. 67g/分 While stirring at room temperature (22 ° C.), CF = CFOCF CF SO CI was added at 1.67 g / min.
2 2 2 2 2 2 2 2
の速度で滴下した。反応の進行と共に溶液が白濁し始め、滴下の間に、発熱により 液温が 22°Cから 33°Cに上昇した。滴下終了後から約 1時間、攪拌して反応を進行さ せた。 At a speed of. The solution began to become cloudy as the reaction progressed, and during the dropwise addition, the temperature of the solution rose from 22 ° C to 33 ° C due to heat generation. The reaction was allowed to proceed for about 1 hour with stirring after the completion of the dropwise addition.
[0056] 反応終了後、フラスコ内は、 Et N : (HF) n (n=4— 6) (液相)/ Et N : HC1 (固相) After completion of the reaction, the inside of the flask contains Et N: (HF) n (n = 4-6) (liquid phase) / Et N: HC1 (solid phase)
3 3 3 3
/CF =CFOCF CF SO F (液相)の 3相分液状態であった。ガスクロマトグラフィ / CF = CFOCF CF SO F (liquid phase) in a three-phase liquid separation state. Gas chromatography
2 2 2 2 2 2 2 2
一及び NMR測定を行なった結果、最下相のみに目的化合物である CF =CF〇CF As a result of the first and NMR measurements, the target compound CF = CF
2 2
CF SO Fが存在していることが確認できた。 CF =CF〇CF CF SO CIの転化率 は 100%、 CF =CF〇CF CF SO Fの選択率は 100%であった。 It was confirmed that CF SO F was present. CF = CF〇CF CF SO CI conversion Was 100%, and the selectivity of CF = CF〇CF CF SO F was 100%.
2 2 2 2 2 2 2 2
[0057] 反応器を加熱して、単蒸留で CF =CFOCF CF SO Fを蒸留回収した結果、 CF [0057] As a result of heating the reactor and distilling and recovering CF = CFOCF CF SO F by simple distillation, CF
2 2 2 2 2 2 2 2
= CF〇CF CF SO Fの単離収率は 96.0%であった。 = The isolation yield of CF FCF CF SO F was 96.0%.
2 2 2 2 2 2 2 2
[0058] フッ素化剤の再牛 [0058] Re-cattle of fluorinating agent
上記方法で得られた Et N: (HF)n(n = 4 6) (液相)/ Et N:HC1(固相)の二相 Et N obtained by the above method: (HF) n (n = 46) (liquid phase) / Et N: HC1 (solid phase)
3 3 3 3
力、らなる混合物 34.6gを 100mlの SUS製オートクレーブ (コンデンサ付き (_10。Cに 冷却))に仕込み、反応系内を真空置換した。その後、 HFをガスとして 10.8g(Et N: A 34.6 g mixture of the force and the mixture was charged into a 100 ml SUS autoclave (with a condenser (_10. Cooled to C)), and the inside of the reaction system was replaced with a vacuum. Then, 10.8 g (Et N:
3 Three
HC1に対して 8倍当量)仕込んで反応させた。 (8 equivalents to HC1) and reacted.
[0059] 副生する HC1ガスは水洗塔を通してトラップした。 HFを 6. lg(0.30mol) (Et N: [0059] By-product HC1 gas was trapped through the washing tower. HF to 6.lg (0.30mol) (Et N:
3 Three
HC1に対して 4.5倍モル量)仕込んだところで圧力が上昇し始め、 0. IMPa (ゲージ 圧)に到達した。この時点で、 HFが仕込めなくなつたので、系内ガスを大気圧付近ま で抜き出しながら HFを仕込んでいった。最終的に仕込んだ HF量は 10.3g(0.52 mol)であった。反応器内の液を NMRで分析したところ Et N:7.7HFが生成してい The pressure began to rise when charged (4.5 times the molar amount of HC1), and reached 0. IMPa (gauge pressure). At this point, HF could not be charged, so HF was charged while extracting gas in the system up to near atmospheric pressure. The final amount of HF charged was 10.3 g (0.52 mol). When the liquid in the reactor was analyzed by NMR, Et N: 7.7HF was generated.
3 Three
た。この Et N:7.7HFを Et N:3HFに戻すために、 15mmHgの減圧下で Et N(H It was. In order to convert this Et N: 7.7HF back to Et N: 3HF, Et N (H
3 3 3 3 3 3
F) の回収を行なった。還流温度 70°Cで安定するまで HFを抜き出し、 70°C留分のF) was collected. Withdraw HF until it is stable at reflux temperature 70 ° C,
3 Three
液について分析した結果、 Et N:3.2HFであった。 As a result of analyzing the liquid, it was Et N: 3.2HF.
[0060] 実施例 2 Example 2
CF =CFOCF CF SO Fの製造 Production of CF = CFOCF CF SO F
2 2 2 2 2 2 2 2
トリェチルァミン 3フッ酸塩(Et N: (HF) )5.4g(33.7mmol)と CF =CFOCF Triethylamine trifluoride (Et N: (HF)) 5.4 g (33.7 mmol) and CF = CFOCF
3 3 2 2 3 3 2 2
CF SO CI 10. lg(33.7mmol)を原料として用い、実施例 1と同様の条件で、 CF CF SO CI 10.Using lg (33.7 mmol) as a raw material, under the same conditions as in Example 1, CF
2 2 twenty two
= CFOCF CF SO Fの合成と単離を行った。この場合、仕込みモル比は 1:1であ = CFOCF CF SO F was synthesized and isolated. In this case, the charged molar ratio is 1: 1.
2 2 2 2 2 2 2 2
る。 The
[0061] 反応の結果、 CF =CFOCF CF SO CIの転化率は 41.9%、 CF =CFOCF C [0061] As a result of the reaction, the conversion of CF = CFOCF CF SO CI was 41.9%, and CF = CFOCF C
2 2 2 2 2 2 2 2 2 2 2 2
F SO Fの選択率は 100%、 CF =CFOCF CF SO Fの単離収率は 38.3%であつThe selectivity of FSOF is 100%, and the isolation yield of CF = CFOCF CFSOF is 38.3%.
2 2 2 2 2 2 2 2 2 2 2 2
た。 It was.
[0062] 実施例 3 Example 3
CF =CFOCF CF SO Fの製诰 CF = CFOCF CF SO F
2 2 2 2 2 2 2 2
100mlの PFA (テトラフルォロエチレンとパーフルォロプロピルビュルエーテルとの 共重合体)製ボトルに、ピリジン 3フッ酸(C H N : (HF) )を 5· 3g(37. 8mmol)仕込 100 ml of PFA (tetrafluoroethylene and perfluoropropyl butyl ether 5.3 g (37.8 mmol) of pyridine 3-hydrofluoric acid (CHN: (HF))
6 5 3 6 5 3
み、そこに純度 82· 5mass%の CF =CFOCF CF SO CIを 4. 7g (13. lmmol) 4.7 g (13.lmmol) of CF = CFOCF CF SO CI with a purity of 82.5 mass%
2 2 2 2 2 2 2 2
を仕込んだ (仕込みモル比 2.9: 1)。この溶液を室温下 (22°C)で 17時間撹拌して反応 を進行させた。 (A molar ratio of 2.9: 1). The solution was stirred at room temperature (22 ° C) for 17 hours to allow the reaction to proceed.
反応終了後、 PFAボトル内は、 C H N : (HF) n (n=4 6) (液相)/ CF =CF〇C After the reaction, the PFA bottle contains C H N: (HF) n (n = 46) (liquid phase) / CF = CF〇C
6 5 2 6 5 2
F CF SO F (液相)の 2相分液状態であった。ガスクロマトグラフィー及び NMR測定 It was a two-phase liquid separation state of F CF SO F (liquid phase). Gas chromatography and NMR measurement
2 2 2 2 2 2
を行なった結果、最下相に目的化合物である CF =CFOCF CF SO Fが存在して As a result, the target compound CF = CFOCF CF SO F
2 2 2 2 2 2 2 2
いることが確認できた。 CF =CF〇CF CF SO CIの転化率は 80. 3%、 CF =CF Was confirmed. CF = CF 〇 CF CF SO CI conversion is 80.3%, CF = CF
2 2 2 2 2 2 2 2 2 2
OCF CF SO Fの選択率は 100%であった。 The selectivity of OCF CF SO F was 100%.
Claims
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|---|---|---|---|
| JP2005517457A JP4379623B2 (en) | 2004-02-02 | 2005-01-26 | Method for producing fluorine-containing unsaturated sulfonyl fluoride |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2004025768 | 2004-02-02 | ||
| JP2004-025768 | 2004-02-02 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2005073182A1 true WO2005073182A1 (en) | 2005-08-11 |
Family
ID=34823996
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/JP2005/001005 Ceased WO2005073182A1 (en) | 2004-02-02 | 2005-01-26 | Method for producing fluorine-containing unsaturated sulfonyl fluoride |
Country Status (2)
| Country | Link |
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| JP (1) | JP4379623B2 (en) |
| WO (1) | WO2005073182A1 (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH1149742A (en) * | 1997-08-01 | 1999-02-23 | Daikin Ind Ltd | Method for producing 2- (trifluoromethylthio) biphenyl, synthetic intermediate thereof and method for producing the same |
| JP2002531426A (en) * | 1998-11-30 | 2002-09-24 | ゾルファイ フルーオル ウント デリヴァーテ ゲゼルシャフト ミット ベシュレンクテル ハフツング | Process for producing oxyfluoride from acid chloride |
| JP2003525286A (en) * | 2000-03-03 | 2003-08-26 | メルク パテント ゲゼルシャフト ミット ベシュレンクテル ハフトング | Production of liquid crystal having CF2O bond |
| JP2004018454A (en) * | 2002-06-14 | 2004-01-22 | Daikin Ind Ltd | Method for producing fluorine-containing fluorosulfonylalkyl vinyl ether |
| JP2004018427A (en) * | 2002-06-14 | 2004-01-22 | Daikin Ind Ltd | Method for producing fluorine-containing fluorosulfonylalkyl vinyl ether |
| JP2004026728A (en) * | 2002-06-26 | 2004-01-29 | Daikin Ind Ltd | Method for producing fluorine-containing fluorosulfonylalkyl vinyl ether |
-
2005
- 2005-01-26 JP JP2005517457A patent/JP4379623B2/en not_active Expired - Fee Related
- 2005-01-26 WO PCT/JP2005/001005 patent/WO2005073182A1/en not_active Ceased
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH1149742A (en) * | 1997-08-01 | 1999-02-23 | Daikin Ind Ltd | Method for producing 2- (trifluoromethylthio) biphenyl, synthetic intermediate thereof and method for producing the same |
| JP2002531426A (en) * | 1998-11-30 | 2002-09-24 | ゾルファイ フルーオル ウント デリヴァーテ ゲゼルシャフト ミット ベシュレンクテル ハフツング | Process for producing oxyfluoride from acid chloride |
| JP2003525286A (en) * | 2000-03-03 | 2003-08-26 | メルク パテント ゲゼルシャフト ミット ベシュレンクテル ハフトング | Production of liquid crystal having CF2O bond |
| JP2004018454A (en) * | 2002-06-14 | 2004-01-22 | Daikin Ind Ltd | Method for producing fluorine-containing fluorosulfonylalkyl vinyl ether |
| JP2004018427A (en) * | 2002-06-14 | 2004-01-22 | Daikin Ind Ltd | Method for producing fluorine-containing fluorosulfonylalkyl vinyl ether |
| JP2004026728A (en) * | 2002-06-26 | 2004-01-29 | Daikin Ind Ltd | Method for producing fluorine-containing fluorosulfonylalkyl vinyl ether |
Also Published As
| Publication number | Publication date |
|---|---|
| JP4379623B2 (en) | 2009-12-09 |
| JPWO2005073182A1 (en) | 2007-09-06 |
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