JPS6112896B2 - - Google Patents

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Publication number
JPS6112896B2
JPS6112896B2 JP53090966A JP9096678A JPS6112896B2 JP S6112896 B2 JPS6112896 B2 JP S6112896B2 JP 53090966 A JP53090966 A JP 53090966A JP 9096678 A JP9096678 A JP 9096678A JP S6112896 B2 JPS6112896 B2 JP S6112896B2
Authority
JP
Japan
Prior art keywords
group
acid ester
reaction
fluoride
metal fluoride
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
JP53090966A
Other languages
Japanese (ja)
Other versions
JPS5519212A (en
Inventor
Shozo Kato
Toshihisa Suyama
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.)
Tokuyama Corp
Original Assignee
Tokuyama Corp
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 Tokuyama Corp filed Critical Tokuyama Corp
Priority to JP9096678A priority Critical patent/JPS5519212A/en
Publication of JPS5519212A publication Critical patent/JPS5519212A/en
Publication of JPS6112896B2 publication Critical patent/JPS6112896B2/ja
Granted legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は含フルオロカルボン酸エステルの製造
方法に関する。 パーフルオロカルボン酸エステルに代表される
含フルオロカルボン酸エステルは、たとえば米国
特許第2567011号明細書に見られる如く、熱安定
性に加えて低表面エネルギー特性を有しているた
めに種々の用途例があり、また合成中間体として
も重要な化合物である。 従来パーフルオロカルボン酸エステルは、カル
ボン酸ならびにその誘導体などを電解フツ素化し
て得られるパーフルオロカルボン酸フルオリドに
アルコールを反応させるか、あるいは、パーフル
オロオレフインなどを酸化して得られるパーフル
オロカルボン酸を濃鉱酸触媒の存在下にアルコー
ルを反応させることにより製造されるのが一般的
であつた。前者における製造法においては毒性が
強く取り扱い難いフツ化水素が発生する難点があ
り、また後者における製造法においてもかなりの
量の濃鉱酸の存在下に加熱しなければならないと
言う難点があつた。先に本発明者らはヘキサフル
オロプロピレンとハロゲン化蟻酸エステルとに金
属フツ化物を加えた系では温和な条件下容易に一
段でヘプタフルオロイソ酪酸エステルが製造でき
ることを見出してその製造方法を完成して既に提
供した。本発明者らはさらに詳細にパーフルオロ
カルボン酸エステルの製造方法について鋭意研究
を重ねた結果、本発明の含フルオロケト酸エステ
ルを金属フツ化物の存在下に非プロトン性溶媒中
で加熱して脱ケト反応を起こさせることによりパ
ーフルオロカルボン酸エステルが好収率で製造で
きることを見出し、本発明をを完成させ提供する
に至つた。 本発明で用いる原料は一般式
The present invention relates to a method for producing a fluorocarboxylic acid ester. Fluorocarboxylic acid esters, represented by perfluorocarboxylic acid esters, have a variety of applications because they have low surface energy properties in addition to thermal stability, as shown in US Pat. It is also an important compound as a synthetic intermediate. Conventionally, perfluorocarboxylic acid esters are perfluorocarboxylic acids obtained by reacting alcohol with perfluorocarboxylic acid fluoride obtained by electrolytic fluorination of carboxylic acids and their derivatives, or by oxidizing perfluoroolefins. was generally produced by reacting an alcohol in the presence of a concentrated mineral acid catalyst. The former production method had the disadvantage of generating hydrogen fluoride, which was highly toxic and difficult to handle, and the latter production method also had the disadvantage of requiring heating in the presence of a considerable amount of concentrated mineral acid. . Previously, the present inventors discovered that heptafluoroisobutyric acid ester could be easily produced in one step under mild conditions using a system in which a metal fluoride was added to hexafluoropropylene and a halogenated formate, and completed the production method. has already been provided. The present inventors conducted intensive research on the method for producing perfluorocarboxylic acid esters in more detail. As a result, the fluoroketo acid esters of the present invention were deketated by heating in an aprotic solvent in the presence of a metal fluoride. The inventors have discovered that perfluorocarboxylic acid esters can be produced in good yield by causing the reaction, and have completed and provided the present invention. The raw materials used in the present invention have the general formula

【式】で示さ れる化合物で、その製法の如何にかかわらず使用
できる。上記式中のRfはフツ素原子あるいは直
鎖または分枝状パーフルオロアルキル基すなわち
トリフルオロメチル基、ペンタフルオロエチル
基、ヘプタフルオロイソプロピル基等の炭素原子
数1〜7好ましくは1〜3のものが一般に用いら
れる。また、上記式中のRは炭化水素残基を指
す。すなわち前記一般式中Rは上記の炭化水素残
基であれば特に限定されず必要に応じて選択でき
るが、一般にはメチル基、エチル基、イソアミル
基、オクチル基、ノニル基など炭素数1から20好
ましくは1から12の直鎖または分枝状アルキル
基;アリル基などのアルケニル基;シクロヘキシ
ル基などのシクロアルキル基;フエネチル基など
のアラルキル基;フエニル基などが好適である。
またこれらの炭化水素残基において水素原子の1
つまたは2つ以上を他の原子または原子団で置換
して誘導された基も好適に使用できる。該水素原
子と置換する原子または原子団は特に限定されな
いが、脱カルボニル反応を起こす条件下において
不活性なものがより好ましく、たとえばフツ素、
塩素、シユウ素などのハロゲン;エステル;スル
ホン酸エステル;ケトン、チオケトン、エーテ
ル;チオエーテル;アルデヒドなどの原子または
原子団が好適である。 本発明で用いる金属フツ化物は前記含フルオロ
ケト酸エステルの脱ケト反応の触媒作用をするも
のである。該金属フツ化物としてはアルカリ金
属、アルカリ土類金属のフツ化物が知られている
が本発明に於いてはこれらの公知の金属フツ化物
が使用出来る。特にフツ化セシウム、フツ化カリ
ウム等のアルカリ金属フツ化物は好適である。ま
たこれらの金属フツ化物を混合して用いることも
出来る。 本発明の反応を化学式で示せば次のようにな
る。 即ち含フルオロケト酸エステルが金属フツ化物
触媒によつて加熱下に脱ケト反応されて対応する
カルボン酸エステルとなる。 本発明における反応即ち脱ケト反応は通常溶媒
の存在下に実施するのが一般的である。該溶媒と
してはジグライム、トリグライム、テトラグライ
ム、スルホラン、ジメチルホルムアミド、ヘキサ
メチルホスホトリアミド、ジメチルスルホキシ
ド、アセトニトリル、N−メチルピロリドンなど
が好ましく、特に好収率で脱ケト反応生成物を得
ると言う点においてはグライム系溶媒が好適であ
る。 本発明に於ける加熱条件は種々の条件例えば原
料の種類、金属フツ化物の種類等によつて異なり
一概に限定することは出来ない。例えば金属フツ
化物としてフツ化セシウムを用いる場合は60℃以
上好ましくは80℃以上で脱ケト反応が進行するが
フツ化カリウムを用いる場合は130℃以上に加熱
するのが好ましい。また加熱温度が高すぎると原
料或いは反応生成物が分解する場合があるのであ
まり高い反応温度を採用しない方が好ましい場合
もある。従つて本発明に於ける反応温度は原料の
種類、金属フツ化物の種類、反応生成物等の性状
に応じて予め好適な加熱温度を決定するのがよ
い。該反応温度は金属フツ化物としてフツ化セシ
ウムを用いる場合は一般に60℃から200℃までの
広い範囲から選択できるが、通常80℃から150℃
の間で行なうのが好ましい。また金属フツ化物と
して他の金属フツ化物を用いる場合は130℃以上
とするのが好ましい。圧力は加圧、常圧、減圧下
いずれでもよいが、常圧で行なうのが操作上簡便
である。反応時間は特に限定されず、数分から数
日の間で選択できるが、一般には数時間で充分で
ある。反応容器の種類は特に限定されず、ガラ
ス、金属製などが好適に使用される。前記一般式
A compound represented by the formula can be used regardless of its manufacturing method. Rf in the above formula is a fluorine atom or a linear or branched perfluoroalkyl group having 1 to 7 carbon atoms, preferably 1 to 3 carbon atoms, such as a trifluoromethyl group, a pentafluoroethyl group, or a heptafluoroisopropyl group. is commonly used. Moreover, R in the above formula refers to a hydrocarbon residue. That is, R in the above general formula is not particularly limited as long as it is the above-mentioned hydrocarbon residue and can be selected as necessary, but generally it is a group having 1 to 20 carbon atoms, such as a methyl group, ethyl group, isoamyl group, octyl group, or nonyl group. Preferably, 1 to 12 linear or branched alkyl groups; alkenyl groups such as allyl groups; cycloalkyl groups such as cyclohexyl groups; aralkyl groups such as phenethyl groups; and phenyl groups are suitable.
Also, one of the hydrogen atoms in these hydrocarbon residues
Groups derived by substituting one or more atoms with other atoms or atomic groups can also be suitably used. The atom or atomic group that replaces the hydrogen atom is not particularly limited, but is preferably inert under the conditions that cause the decarbonylation reaction, such as fluorine,
Preferred are atoms or atomic groups such as halogens such as chlorine and silium; esters; sulfonic acid esters; ketones, thioketones, ethers; thioethers; aldehydes. The metal fluoride used in the present invention catalyzes the deketo reaction of the fluoroketo acid ester. As the metal fluoride, fluorides of alkali metals and alkaline earth metals are known, and these known metal fluorides can be used in the present invention. Particularly suitable are alkali metal fluorides such as cesium fluoride and potassium fluoride. It is also possible to use a mixture of these metal fluorides. The reaction of the present invention can be expressed as a chemical formula as follows. That is, the fluoroketo acid ester is subjected to a deketo reaction under heating using a metal fluoride catalyst to form the corresponding carboxylic acid ester. The reaction in the present invention, that is, the ketosis removal reaction, is generally carried out in the presence of a solvent. As the solvent, diglyme, triglyme, tetraglyme, sulfolane, dimethylformamide, hexamethylphosphotriamide, dimethylsulfoxide, acetonitrile, N-methylpyrrolidone, etc. are preferable, especially in that they yield the deketotic reaction product in a good yield. In this case, glyme-based solvents are suitable. The heating conditions in the present invention vary depending on various conditions, such as the type of raw material, the type of metal fluoride, etc., and cannot be absolutely limited. For example, when cesium fluoride is used as the metal fluoride, the ketosis-removal reaction proceeds at 60°C or higher, preferably 80°C or higher, but when potassium fluoride is used, it is preferably heated to 130°C or higher. Furthermore, if the heating temperature is too high, the raw materials or reaction products may decompose, so it may be preferable not to use a too high reaction temperature. Therefore, it is preferable to determine a suitable heating temperature in advance for the reaction temperature in the present invention depending on the type of raw material, the type of metal fluoride, the properties of the reaction product, etc. The reaction temperature can generally be selected from a wide range of 60°C to 200°C when cesium fluoride is used as the metal fluoride, but it is usually 80°C to 150°C.
It is preferable to do this between Further, when using another metal fluoride as the metal fluoride, the temperature is preferably 130°C or higher. Although the pressure may be increased, normal pressure, or reduced pressure, it is operationally convenient to carry out the reaction at normal pressure. The reaction time is not particularly limited and can be selected from several minutes to several days, but generally several hours is sufficient. The type of reaction vessel is not particularly limited, and those made of glass, metal, etc. are preferably used. The above general formula

【式】で示される含フルオロケト酸エステル と触媒として用いる金属フツ化物との仕込みモル
比は、前者の構造、反応性に応じて異なるので必
要に応じて適宜選定すればよいが、通常、前者に
対し、金属フツ化物を0.1〜100モル%の間で用い
れば好ましい。 また、反応時に金属フツ化物を均一に分散させ
る手段として反応混合物を撹拌することは好まし
い態様である。 本発明を更に具体的に説明するために以下の実
施例を示すが、本発明はこれらの実施例に限定さ
れるものではない。なお、実施例における反応収
率は原料に用いた含フルオロケト酸エステルの重
量に対し、反応混合物から蒸留により単離された
対応する含フルオロカルボン酸エステルの重量を
もつて算出した。 実施例 1 30mlナス型フラスコにフツ化セシウム1.1g、
ヘプタフルオロイソプロピルグリオギザル酸β−
エトキシエチル4.5g、テトラグライム8mlを入
れ、油浴上100〜115℃に3時間加熱撹拌した。反
応混合物を減圧蒸留することにより、沸点36.5
℃/6.5mmHgのヘプタフルオロイソ酪酸β−エト
キシエチル2.92gを得た。収率は71.5%であつ
た。 実施例 2 実施例1のヘプタフルオロイソプロピルグリオ
キザル酸β−エトキシエチルの代わりに表1に示
す含フルオロケト酸エステルを用い、表1に示す
反応条件とした以外は実施例1と同様に実施し、
生成物である含フルオロカルボン酸エステルを得
た。単離した生成物の収率および沸点は表1に示
す通りであつた。
The molar ratio of the fluoroketo acid ester represented by [Formula] and the metal fluoride used as a catalyst varies depending on the structure and reactivity of the former, so it may be selected as necessary. On the other hand, it is preferable to use the metal fluoride in an amount of 0.1 to 100 mol %. Furthermore, it is a preferred embodiment to stir the reaction mixture as a means to uniformly disperse the metal fluoride during the reaction. The following examples are shown to further specifically explain the present invention, but the present invention is not limited to these examples. In addition, the reaction yield in the examples was calculated by calculating the weight of the corresponding fluorocarboxylic acid ester isolated by distillation from the reaction mixture with respect to the weight of the fluoroketo acid ester used as a raw material. Example 1 1.1g of cesium fluoride in a 30ml eggplant flask,
Heptafluoroisopropylglyogyzalic acid β-
4.5 g of ethoxyethyl and 8 ml of tetraglyme were added, and the mixture was heated and stirred on an oil bath at 100 to 115°C for 3 hours. By distilling the reaction mixture under reduced pressure, the boiling point was 36.5.
2.92 g of β-ethoxyethyl heptafluoroisobutyrate was obtained at a temperature of 6.5 mmHg. The yield was 71.5%. Example 2 The same procedure as in Example 1 was carried out, except that the fluoroketo acid ester shown in Table 1 was used instead of β-ethoxyethyl heptafluoroisopropylglyoxalate in Example 1, and the reaction conditions shown in Table 1 were used.
A product, a fluorocarboxylic acid ester, was obtained. The yield and boiling point of the isolated product were as shown in Table 1.

【表】【table】

【表】【table】

【表】【table】

【表】【table】

Claims (1)

【特許請求の範囲】 1 一般式【式】(但しRfは直鎖または分 枝状パーフルオロアルキル基あるいはフツ素原
子;Rは炭化水素残基)で示される含フルオロケ
ト酸エステルを金属フツ化物の存在下に非プロト
ン性溶媒中で加熱することを特徴とする含フルオ
ロカルボン酸エステルの製造方法。 2 一般式中のRfがヘプタフルオロイソプロピ
ル基〔(CF32CF〕、ペンタフルオロエチル基
(CF3CF2)、トリフルオロメチル基(CF3)または
フツ素原子である特許請求の範囲1記載の方法。 3 一般式中のRが直鎖状または分枝状のアルキ
ル基、アルケニル基、シクロアルキル基またはフ
エニル基である特許請求の範囲1記載の方法。 4 金属フツ化物が、フツ化セシウム又はフツ化
カリウムである特許請求の範囲1記載の方法。 5 非プロトン性溶媒がグライム系溶媒である特
許請求の範囲1記載の方法。 6 加熱温度が60〜200℃の範囲から選ばれる特
許請求の範囲1記載の方法。
[Claims] 1. A fluoroketo acid ester represented by the general formula [Formula] (where Rf is a linear or branched perfluoroalkyl group or a fluorine atom; R is a hydrocarbon residue) as a metal fluoride. A method for producing a fluorocarboxylic acid ester, which comprises heating in an aprotic solvent in the presence of a fluorocarboxylic acid ester. 2 Claim 1 in which Rf in the general formula is a heptafluoroisopropyl group [(CF 3 ) 2 CF], a pentafluoroethyl group (CF 3 CF 2 ), a trifluoromethyl group (CF 3 ), or a fluorine atom Method described. 3. The method according to claim 1, wherein R in the general formula is a linear or branched alkyl group, alkenyl group, cycloalkyl group, or phenyl group. 4. The method according to claim 1, wherein the metal fluoride is cesium fluoride or potassium fluoride. 5. The method according to claim 1, wherein the aprotic solvent is a glyme-based solvent. 6. The method according to claim 1, wherein the heating temperature is selected from the range of 60 to 200°C.
JP9096678A 1978-07-27 1978-07-27 Preparation of fluoro-containing carboxylic acid ester Granted JPS5519212A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9096678A JPS5519212A (en) 1978-07-27 1978-07-27 Preparation of fluoro-containing carboxylic acid ester

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9096678A JPS5519212A (en) 1978-07-27 1978-07-27 Preparation of fluoro-containing carboxylic acid ester

Publications (2)

Publication Number Publication Date
JPS5519212A JPS5519212A (en) 1980-02-09
JPS6112896B2 true JPS6112896B2 (en) 1986-04-10

Family

ID=14013230

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9096678A Granted JPS5519212A (en) 1978-07-27 1978-07-27 Preparation of fluoro-containing carboxylic acid ester

Country Status (1)

Country Link
JP (1) JPS5519212A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6416490A (en) * 1987-07-10 1989-01-19 Yasunaga Sangyo Kk Diving work equipment

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6416490A (en) * 1987-07-10 1989-01-19 Yasunaga Sangyo Kk Diving work equipment

Also Published As

Publication number Publication date
JPS5519212A (en) 1980-02-09

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