JPH0155261B2 - - Google Patents

Info

Publication number
JPH0155261B2
JPH0155261B2 JP1661784A JP1661784A JPH0155261B2 JP H0155261 B2 JPH0155261 B2 JP H0155261B2 JP 1661784 A JP1661784 A JP 1661784A JP 1661784 A JP1661784 A JP 1661784A JP H0155261 B2 JPH0155261 B2 JP H0155261B2
Authority
JP
Japan
Prior art keywords
fluorine
production method
acid derivative
elimination reaction
reduced pressure
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP1661784A
Other languages
Japanese (ja)
Other versions
JPS60158137A (en
Inventor
Masahiro Suefuji
Shinichi Imazu
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Daikin Industries Ltd
Original Assignee
Daikin Industries Ltd
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 Daikin Industries Ltd filed Critical Daikin Industries Ltd
Priority to JP1661784A priority Critical patent/JPS60158137A/en
Publication of JPS60158137A publication Critical patent/JPS60158137A/en
Publication of JPH0155261B2 publication Critical patent/JPH0155261B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は、含フツ素アクリル酸誘導体の製法に
関し、更に詳しくは含フツ素プロピオン酸から脱
ハロゲンすることから成る含フツ素アクリル酸誘
導体の製法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a fluorine-containing acrylic acid derivative, and more particularly to a method for producing a fluorine-containing acrylic acid derivative, which comprises dehalogenating fluorine-containing propionic acid.

一般式:=CH2=CFCOY (1) (式中、Yはハロゲンまたは低級アルコキシ基を
表わす。) で示される含フツ素アクリル酸誘導体は、医薬
(たとえば抗生物質)の中間体、光学繊維のさや
材用材料の中間体、塗料用材料の中間体、更に半
導体レジスト材料の中間体として有用である。
The fluorine-containing acrylic acid derivative represented by the general formula: =CH 2 =CFCOY (1) (in the formula, Y represents a halogen or lower alkoxy group) is used as an intermediate for pharmaceuticals (such as antibiotics) and as an optical fiber. It is useful as an intermediate for sheath materials, a paint material intermediate, and a semiconductor resist material intermediate.

従来該化合物(1)、たとえば、α−フルオロアク
リル酸エステルは、α,α,β−トリブロモプロ
ピオン酸エステルをフツ化水銀でフツ素化して
α,β−ジブロモ−α−フルオロプロピオン酸を
得、これを脱臭素する方法(ジヤーナル・オブ・
ケミカル・ソサエテイ、第75巻、第479〜481頁、
1954年発行)や、モノクロロ酢酸エステルをフツ
化カリウムでフツ素化してモノフルオロ酢酸を
得、次いでこれをエーテル中シユウ酸ジメチルと
反応させ、さらにパラホルムアルデヒド、メトキ
シナトリウムと反応させる方法(マクロモレキユ
ールズ、第13巻、第1031〜1036頁、1980年発行)
により製造されることが知られている。
Conventionally, the compound (1), for example, α-fluoroacrylic acid ester, is obtained by fluorinating α,α,β-tribromopropionic acid ester with mercury fluoride to obtain α,β-dibromo-α-fluoropropionic acid. , how to debromine this (Journal of
Chemical Society, Vol. 75, pp. 479-481,
(published in 1954), a method in which monofluoroacetic acid is fluorinated with potassium fluoride to obtain monofluoroacetic acid, which is then reacted with dimethyl oxalate in ether, and further reacted with paraformaldehyde and sodium methoxy (macromolecule). Yules, Vol. 13, pp. 1031-1036, published 1980)
It is known that it is manufactured by

しかし、前者の方法では、毒性の強い水銀化合
物を用いなければならず、収率も10%と低く、一
方後者の方法でも、毒性の強いモノフルオロ酢酸
を経由しなければならず、収率も30%程度であ
り、しかも溶媒として引火性の大きなエーテルを
使用することなどの問題がある。
However, the former method requires the use of highly toxic mercury compounds and the yield is as low as 10%, while the latter method also requires the use of highly toxic monofluoroacetic acid and has a low yield. 30%, and there are problems such as the use of highly flammable ether as a solvent.

本発明者らは、該化合物(1)の製法について研究
を行ない、対応する含フツ素プロピオン酸誘導体
を脱ハロゲンすることにより該化合物(1)が容易に
得られることを見い出し、本発明を完成するに至
つた。
The present inventors conducted research on the method for producing the compound (1) and found that the compound (1) can be easily obtained by dehalogenating the corresponding fluorine-containing propionic acid derivative, and completed the present invention. I came to the conclusion.

すなわち、本発明の要旨は、一般式: XCH2CF2COY (2) (式中、Yは前記と同意義。Xはハロゲンを表わ
す。) で示される含フツ素プロピオン酸誘導体から脱ハ
ロゲン化剤の存在下、0〜150℃の温度で 一般式:XF (3) (式中、Xは前記と同意義。) で示されるハロゲン化合物を脱離して 一般式: CH2=CFCOY (1) (式中、Yは前記と同意義。) で示される化合物を得ることを特徴とする含フツ
素アクリル酸誘導体の製法に存する。
That is, the gist of the present invention is to dehalogenate a fluorine-containing propionic acid derivative represented by the general formula: XCH 2 CF 2 COY (2) (wherein, Y has the same meaning as above. In the presence of an agent, at a temperature of 0 to 150°C, the halogen compound represented by the general formula: XF ( 3 ) (wherein, (In the formula, Y has the same meaning as defined above.) A method for producing a fluorine-containing acrylic acid derivative is provided, which is characterized by obtaining a compound represented by the following formula.

出発物質である含フツ素プロピオン酸誘導体(2)
は、たとえば2,2,3,3−テトラフルオロオ
キセタンをヨウ化ナトリウムで処理することによ
り容易に得られる。
Starting material, fluorine-containing propionic acid derivative (2)
is easily obtained, for example, by treating 2,2,3,3-tetrafluorooxetane with sodium iodide.

脱ハロゲン化剤としては、既知のもの、たとえ
ば亜鉛、ナトリウム、マグネシウム、錫、銅、鉄
などが用いられる。
As the dehalogenating agent, known ones such as zinc, sodium, magnesium, tin, copper, iron, etc. can be used.

反応温度は、一般に0〜150℃、好ましくは30
〜80℃、より好ましくは40〜60℃である。
The reaction temperature is generally 0 to 150°C, preferably 30°C.
-80°C, more preferably 40-60°C.

反応圧力は、常圧でもよいが、200mmHg以下、
好ましくは20〜50mmHgの減圧下で行なうと自身
重合しやすい生成物含フツ素アクリル酸誘導体の
重合が防止されてその収率が向上する。
The reaction pressure may be normal pressure, but should not exceed 200 mmHg.
Preferably, when the reaction is carried out under a reduced pressure of 20 to 50 mmHg, polymerization of the product fluorine-containing acrylic acid derivative, which tends to self-polymerize, is prevented and the yield thereof is improved.

また、反応は溶媒中で行なうのが好ましく、溶
媒としては、極性溶媒、たとえばジメチルホルム
アミド(DMF)、アセトニトリル、アセトンなど
が挙げられる。
Further, the reaction is preferably carried out in a solvent, and examples of the solvent include polar solvents such as dimethylformamide (DMF), acetonitrile, and acetone.

本発明においては、反応を環流下に行なつて反
応終了後生成物を減圧蒸留により回収してもよい
が、前記重合防止がより効果的に達成されるとい
う利点から、反応中に生成物を連続的に回収する
のが望ましい。
In the present invention, the reaction may be carried out under reflux and the product may be recovered by distillation under reduced pressure after the completion of the reaction. Continuous collection is desirable.

次ぎに、実施例を示し、本発明の製法を具体的
に説明する。
Next, the manufacturing method of the present invention will be specifically explained with reference to Examples.

実施例 1 5l四つ口フラスコ中、亜鉛373gのDMF2500g
懸濁液に50〜60℃でICH2CF2COF1042g(4.378
モル)を滴下した後、1時間撹拌した。次いで、
反応混合物を42〜45℃、50mmHgで減圧単蒸留し
て粗CH2=CFCOF162gを得た。収率37.6%。ガ
スクロマトグラフイによる純度分析は93.5%であ
つた。
Example 1 2500 g of DMF with 373 g of zinc in a 5l four-necked flask
1042 g of ICH 2 CF 2 COF (4.378
mol) was added dropwise, and the mixture was stirred for 1 hour. Then,
The reaction mixture was subjected to simple distillation under reduced pressure at 42-45° C. and 50 mmHg to obtain 162 g of crude CH 2 =CFCOF. Yield 37.6%. Purity analysis by gas chromatography was 93.5%.

実施例 2 実施例1と同様の仕込量を用いたが、
ICH2CF2COFは50〜60℃、20mmHgの減圧下に環
流しながら滴下した。滴下終了後、実施例1と同
様に減圧蒸留して粗CH2=CFCOF274gを得た。
収率62.0%。ガスクロマトグラフイによる純度分
析は91.2%であつた。
Example 2 The same loading amount as in Example 1 was used, but
ICH 2 CF 2 COF was added dropwise at 50 to 60° C. under reduced pressure of 20 mmHg while refluxing. After completion of the dropwise addition, vacuum distillation was performed in the same manner as in Example 1 to obtain 274 g of crude CH 2 =CFCOF.
Yield 62.0%. Purity analysis by gas chromatography was 91.2%.

実施例 3 減圧度を40mmHg、反応温度を50〜60℃とし、
生成物を蒸留塔頂温度38〜40℃で連続的に回収す
る以外は実施例2の手順を繰り返して、粗CH2
CFCOF343gを得た。収率80.6%。ガスクロマト
グラフイによる純度分析は94.8%であつた。
Example 3 The degree of reduced pressure was 40 mmHg, the reaction temperature was 50 to 60°C,
The procedure of Example 2 was repeated except that the product was continuously recovered at a distillation overhead temperature of 38-40° C. to produce crude CH 2 =
343g of CFCOF was obtained. Yield 80.6%. Purity analysis by gas chromatography was 94.8%.

実施例 4 1l四つ口フラスコ中、亜鉛93gのアセトニトリ
ル500g懸濁液に50〜60℃で
BrCH2CF2COOCH3194g(0.956モル)を滴下し
た後、1時間撹拌した。次いで、反応混合物を減
圧単蒸留して粗CH2=CFCOOCH340.7gを得た。
GC−MS:104(M+)、59(COOCH3)、45(CH2
CF)。
Example 4 A suspension of 93 g of zinc in 500 g of acetonitrile at 50-60°C in a 1 L four-necked flask.
After 194 g (0.956 mol) of BrCH 2 CF 2 COOCH 3 was added dropwise, the mixture was stirred for 1 hour. Then, the reaction mixture was subjected to simple distillation under reduced pressure to obtain 40.7 g of crude CH 2 =CFCOOCH 3 .
GC-MS: 104 (M + ), 59 (COOCH 3 ), 45 (CH 2 =
CF).

実施例 5 1l四つ口フラスコ中、亜鉛70gのDMF500g懸
濁液に50〜60℃でICH2CF2COCl210g(0.825モ
ル)を滴下した後、1時間撹拌した。次いで、反
応混合物を減圧単蒸留して粗CH2=CFCOCl49.5
gを得た。GC−MS:108(M+)、63(COCl)、45
(CH2=CF)。
Example 5 210 g (0.825 mol) of ICH 2 CF 2 COCl was added dropwise to a suspension of 70 g of zinc in 500 g of DMF at 50 to 60° C. in a 1-liter four-necked flask, followed by stirring for 1 hour. The reaction mixture was then subjected to simple distillation under reduced pressure to obtain crude CH 2 =CFCOCl49.5
I got g. GC−MS: 108 (M + ), 63 (COCl), 45
( CH2 =CF).

Claims (1)

【特許請求の範囲】 1 一般式: XCH2CF2COY (式中、Xはハロゲン、Yはハロゲンまたは低級
アルコキシ基を表わす。) で示される含フツ素プロピオン酸誘導体から、脱
ハロゲン化剤の存在下、0〜150℃の温度で 一般式:XF (式中、Xは前記と同意義。) で示されるハロゲン化合物を脱離して 一般式: CH2=CFCOY (式中、Yは前記と同意義。) で示される化合物を得ることを特徴とする含フツ
素アクリル酸誘導体の製法。 2 脱離反応を200mmHg以下の減圧下に行なう特
許請求の範囲第1項記載の製法。 3 脱離反応を20〜50mmHgの減圧下に行なう特
許請求の範囲第1項または第2項記載の製法。 4 脱離反応中、含フツ素アクリル酸誘導体を連
続的に回収、取得する特許請求の範囲第1〜3項
のいずれかに記載の製法。 5 脱ハロゲン化剤が、亜鉛、ナトリウム、マグ
ネシウム、錫、銅または鉄である特許請求の範囲
第1〜4項のいずれかに記載の製法。 6 脱離反応を40〜60℃の温度で行なう特許請求
の範囲第1〜5項のいずれかに記載の製法。 7 Yがハロゲンである特許請求の範囲第1〜6
項のいずれかに記載の製法。
[Claims] 1. A dehalogenating agent derived from a fluorine-containing propionic acid derivative represented by the general formula: XCH 2 CF 2 COY (wherein, In the presence of the compound, a halogen compound represented by the general formula: Same meaning.) A method for producing a fluorine-containing acrylic acid derivative, which is characterized by obtaining a compound represented by: 2. The production method according to claim 1, wherein the elimination reaction is carried out under reduced pressure of 200 mmHg or less. 3. The production method according to claim 1 or 2, wherein the elimination reaction is carried out under reduced pressure of 20 to 50 mmHg. 4. The production method according to any one of claims 1 to 3, wherein the fluorine-containing acrylic acid derivative is continuously recovered and obtained during the elimination reaction. 5. The production method according to any one of claims 1 to 4, wherein the dehalogenating agent is zinc, sodium, magnesium, tin, copper, or iron. 6. The production method according to any one of claims 1 to 5, wherein the elimination reaction is carried out at a temperature of 40 to 60°C. 7 Claims 1 to 6 in which Y is halogen
The manufacturing method described in any of the paragraphs.
JP1661784A 1984-01-30 1984-01-30 Preparation of fluorine-containing acrylic acid derivative Granted JPS60158137A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1661784A JPS60158137A (en) 1984-01-30 1984-01-30 Preparation of fluorine-containing acrylic acid derivative

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1661784A JPS60158137A (en) 1984-01-30 1984-01-30 Preparation of fluorine-containing acrylic acid derivative

Publications (2)

Publication Number Publication Date
JPS60158137A JPS60158137A (en) 1985-08-19
JPH0155261B2 true JPH0155261B2 (en) 1989-11-22

Family

ID=11921289

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1661784A Granted JPS60158137A (en) 1984-01-30 1984-01-30 Preparation of fluorine-containing acrylic acid derivative

Country Status (1)

Country Link
JP (1) JPS60158137A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014522398A (en) * 2011-06-01 2014-09-04 ロディア オペレーションズ Method for preparing fluorinated organic compounds

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3915754A1 (en) * 1989-05-13 1990-11-15 Bayer Ag METHOD FOR PRODUCING (ALPHA) FLUORACRYLIC ACID DERIVATIVES AND NEW 1,1-DIFLUOR-2-HALOGENETHYL (HALOGEN) METHYL KETONE
FR2812632B1 (en) * 2000-08-07 2003-03-07 Solvay PROCESS FOR THE SYNTHESIS OF FLUOROORGANIC COMPOUNDS

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014522398A (en) * 2011-06-01 2014-09-04 ロディア オペレーションズ Method for preparing fluorinated organic compounds

Also Published As

Publication number Publication date
JPS60158137A (en) 1985-08-19

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