JP4362908B2 - Production method of monoester from dicarboxylic acid fluoride - Google Patents

Production method of monoester from dicarboxylic acid fluoride Download PDF

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Publication number
JP4362908B2
JP4362908B2 JP31320499A JP31320499A JP4362908B2 JP 4362908 B2 JP4362908 B2 JP 4362908B2 JP 31320499 A JP31320499 A JP 31320499A JP 31320499 A JP31320499 A JP 31320499A JP 4362908 B2 JP4362908 B2 JP 4362908B2
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Japan
Prior art keywords
dicarboxylic acid
monoester
fluoride
foccf
group
Prior art date
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JP31320499A
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Japanese (ja)
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JP2001131119A (en
Inventor
弘明 村多
直 池田
智 斉藤
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Unimatec Co Ltd
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Unimatec Co Ltd
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Priority to JP31320499A priority Critical patent/JP4362908B2/en
Priority to US09/699,656 priority patent/US6407282B1/en
Publication of JP2001131119A publication Critical patent/JP2001131119A/en
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Description

【0001】
【発明の属する技術分野】
本発明は、ジカルボン酸フロライドからのモノエステルの製造法に関する。更に詳しくは、パーフルオロビニルエーテル合成の原料物質として有用なジカルボン酸のモノエステルモノ酸フロライドをジカルボン酸フロライドから製造する方法に関する。
【0002】
【従来の技術】
パーフルオロビニルエーテルは、含フッ素エラストマー等に用いられる有用な単量体であり、それの合成はジカルボンモノエステルモノ酸フロライドの酸フロライド基をカルボン酸塩に変換させた後熱分解反応させることによって行われている(特公昭53-33572〜3号公報)。
FOCCF(CF 3 )O(CF 2 CFXO)p(CF 2 )qCOOR

MOOCCF(CF 3 )O(CF 2 CFXO)p(CF 2 )qCOOR

CF 2 =CFO(CF 2 CFXO)p(CF 2 )qCOOR
【0003】
ここで用いられるジカルボン酸のモノエステルモノ酸フロライドは、一般にジカルボン酸フロライドに等モル量のアルコールを反応させ、一方の酸フロライド基をエステル化することによって行われるが、その場合用いられるアルコールの反応モル比が少ない内は選択率が上がるが、未反応のジカルボン酸フロライドが多く残り、転化率が上らないという問題がある。一方、アルコールの反応モル比を増加させると転化率は上がるが、ジエステルの生成量が多くなり、選択率が低下してくるようになる。
【0004】
【発明が解決しようとする課題】
本発明の目的は、ジカルボン酸フロライドからジカルボン酸のモノエステルモノ酸フロライドを製造するに際し、転化率および選択率をそれぞれ増大せしめ、結果として目的物の収率を改善せしめる方法を提供することにある。
【0005】
【課題を解決するための手段】
かかる本発明の目的は、一般式
FOCCF(CF3)OCF2(A)p(CF2)qCOF
(ここで、Aは炭素数1〜10の二官能性パーフルオロ化基であり、pは0または1であり、そしてqは0または1〜10の整数である)で表わされるジカルボン酸フロライドを、炭素数3以上のアルコールと反応させ、 CF 2 COF 基側をエステル化してジカルボン酸のモノエステルモノ酸フロライドを製造する方法によって達成される。
【0006】
【発明の実施の形態】
上記一般式で表わされる非対称ジカルボン酸フロライドは、一般式 FOC(A)p(CF2)qCOF で表わされるジカルボン酸フロライドにヘキサフルオロプロピレンオキサイドを反応させる方法(米国特許第3,114,778号明細書)あるいはパーフルオロラクトンにヘキサフルオロプロピレンオキサイドを反応させる方法(特開昭53-3017号公報)などによって得られることが、特公昭57-61339号公報に記載されている。
【0007】
ここでAは、分岐または非分岐の二官能性パーフルオロ化基であって、1個またはそれ以上のエーテル結合を含むことができ、例えば次のような一般式で表わされる基であり得る。
-[CF(CF3)OCF2]m(Rf)n-
Rf:炭素数1〜10、好ましくは1〜4の直鎖状または分岐状の
パーフルオロアルキレン基
m:0,1または2
n:0または1
【0008】
このようなジカルボン酸フロライドの例としては、次のような化合物が挙げられる。
FOCCF(CF3)OCF2COF
FOCCF(CF3)O(CF2)2COF
FOCCF(CF3)O(CF2)3COF
FOCCF(CF3)O(CF2)4COF
FOCCF(CF3)O(CF2)5COF
FOCCF(CF3)OCF2CF(CF3)OCF2COF
FOCCF(CF3)OCF2CF(CF3)O(CF2)2COF
FOCCF(CF3)OCF2CF(CF3)O(CF2)3COF
FOCCF(CF3)OCF2CF(CF3)O(CF2)4COF
FOCCF(CF3)OCF2CF(CF3)O(CF2)5COF
【0009】
これらのジカルボン酸フロライドと反応するアルコールとしては、炭素数3以上のアルコール、例えばプロパノール、イソプロパノール、n-ブタノール、イソブタノール(2-ブタノール)、2-メチル-1-プロパノール、4-ヘプタノール、2,2-ジメチル-1-プロパノール、2,4-ジメチル-3-ペンタノール等が用いられ、好ましくは分岐基を有するアルコールが用いられる。
【0010】
これら両者間の反応は、ジカルボン酸フロライド1モルに対して0.7〜2モル、好ましくは約1〜1.5モルのアルコールを用い、約-60〜60℃の反応温度で行われる。反応温度の低い方が選択性は向上するが、冷却装置の能力や経済性などを考慮すれば、約-40〜20℃で反応させることが好ましい。
【0011】
この反応は、溶媒の存在下または不存在下で行うことができ、溶媒を用いる場合には、反応を阻害しない限り任意のものを使用し得るが、ジカルボン酸フロライドの合成段階でも使用されたジグライム、テトラグライム等が好んで用いられる。なお、縮合反応の結果副生されるフッ化水素は、反応系に共存させたフッ化ナトリウム等のアルカリ金属フッ化物によって吸着させることで、反応器の腐食等を抑制することができる。
【0012】
【発明の効果】
パーフルオロビニルエーテルを共重合させた共重合体は、機能性含フッ素ポリマーとして撥水撥油剤等の用途に有効に用いられるが、かかる共重合体の成分としてのパーフルオロビニルエーテルを合成するための中間体であるパーフルオロエーテル結合を有するジカルボン酸のモノエステルモノ酸フロライドFOCCF(CF 3 )OCF 2 (A)p(CF 2 )qCOORが、本発明ではエステル化剤として炭素数3以上のアルコールを選択して用いることにより、好転化率および好選択率で製造することができる。
【0013】
【実施例】
次に、実施例について本発明を説明する。
【0014】
参考例
パーフルオロアジピン酸フロライド327g(1.1モル)、フッ化セシウム15.2g(0.1モル)およびジグライム300mlを用い、0〜5℃でヘキサフルオロプロペンオキシド199.2g(1.2モル)と反応させ、反応混合物を蒸留してジカルボン酸フロライド FOCCF(CF3)O(CF2)5COF を得た。
【0015】
実施例1
容量500mlのガラス製反応容器内に、FOCCF(CF3)O(CF2)5COF 300g(0.65モル)およびフッ化ナトリウム33gを仕込み、内温を-30〜-20℃に保ちながら攪拌を行ない、そこにプロパノール42.9g(0.72モル)を2時間かけて滴下した。滴下終了後、フッ化ナトリウムをロ別し、ガスクロマトグラフィー組成で原料15.8%、モノエステル48.5%およびジエステル35.7%の混合物287gを得た。反応の転化率は84.2%、モノエステルの選択率は57.6%、収率は42.8%であった。
【0016】
実施例2
実施例1において、プロパノールの代りに同量のイソプロパノールを用い、原料11.4%、モノエステル59.1%およびジエステル25.6%の混合物285gを得た。反応の転化率は88.6%、モノエステルの選択率は69.8%、収率は51.8%であった。
【0017】
実施例3
実施例1において、プロパノールの代りに2,2-ジメチル-1-プロパノール63.3g(0.72モル)をテトラグライム30gに溶解させたものを用い、原料6.8%、モノエステル74.0%およびジエステル17.0%の混合物328gを得た。反応の転化率は93.2%、モノエステルの選択率は81.3%、収率は64.3%であった。
【0018】
実施例4
実施例1において、ジカルボン酸フロライドとして FOCCF(CF3)O(CF2)3COF 234g(0.65モル)を用い、またプロパノールの代りに2,4-ジメチル-3-ペンタノール83.5g(0.72モル)を用い、原料5.8%、モノエステル78.4%およびジエステル15.8%の混合物256gを得た。反応の転化率は94.2%、モノエステルの選択率は83.2%、収率は67.7%であった。
【0019】
実施例5
実施例1において、ジカルボン酸フロライドとして FOCCF(CF3)O(CF2)2COF 202g(0.65モル)を用い、またプロパノールの代りに2,4-ジメチル-3-ペンタノール83.5g(0.72モル)を用い、原料6.7%、モノエステル76.6%およびジエステル16.7%の混合物220gを得た。反応の転化率は93.3%、モノエステルの選択率は82.1%、収率は63.9%であった。
【0020】
比較例
実施例1において、プロパノールの代りにメタノール22.9g(0.72モル)を用い、原料19.0%、モノエステル42.9%およびジエステル38.1%の混合物262gを得た。反応の転化率は81.0%、モノエステルの選択率は53.0%、収率は36.6%であった。
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for producing a monoester from dicarboxylic acid fluoride. More specifically, the present invention relates to a method for producing a monoester monoacid fluoride of dicarboxylic acid useful as a raw material for synthesizing perfluorovinyl ether from dicarboxylic acid fluoride.
[0002]
[Prior art]
Perfluorovinyl ether is a useful monomer used for fluorine-containing elastomers and the like, and its synthesis is carried out by converting the acid fluoride group of dicarboxylic monoester monoacid fluoride to a carboxylate and then carrying out a thermal decomposition reaction. (Japanese Patent Publication No. 53-33572-3).
FOCCF (CF 3 ) O (CF 2 CFXO) p (CF 2 ) qCOOR

MOOCCF (CF 3 ) O (CF 2 CFXO) p (CF 2 ) qCOOR

CF 2 = CFO (CF 2 CFXO) p (CF 2 ) qCOOR
[0003]
The monoester monoacid fluoride of dicarboxylic acid used here is generally obtained by reacting dicarboxylic acid fluoride with an equimolar amount of alcohol and esterifying one acid fluoride group. In this case, reaction of the alcohol used The selectivity increases when the molar ratio is small, but there is a problem that a large amount of unreacted dicarboxylic acid fluoride remains and the conversion does not increase. On the other hand, when the reaction molar ratio of alcohol is increased, the conversion rate is increased, but the amount of diester produced is increased and the selectivity is decreased.
[0004]
[Problems to be solved by the invention]
An object of the present invention is to provide a method for increasing the conversion rate and the selectivity in producing a monoester monoacid fluoride of dicarboxylic acid from dicarboxylic acid fluoride, thereby improving the yield of the target product. .
[0005]
[Means for Solving the Problems]
The object of the present invention is to provide a general formula
FOCCF (CF 3 ) OCF 2 (A) p (CF 2 ) qCOF
(Wherein A is a bifunctional perfluorinated group having 1 to 10 carbon atoms, p is 0 or 1, and q is 0 or an integer of 1 to 10). This is achieved by a method of producing a monoester monoacid fluoride of a dicarboxylic acid by reacting with an alcohol having 3 or more carbon atoms and esterifying the CF 2 COF group side .
[0006]
DETAILED DESCRIPTION OF THE INVENTION
The asymmetric dicarboxylic acid fluoride represented by the above general formula is obtained by reacting a dicarboxylic acid fluoride represented by the general formula FOC (A) p (CF 2 ) qCOF with hexafluoropropylene oxide (US Pat. No. 3,114,778) or JP-B-57-61339 discloses that it can be obtained by a method of reacting a fluorolactone with hexafluoropropylene oxide (Japanese Patent Laid-Open No. 53-3017).
[0007]
Here, A is a branched or unbranched bifunctional perfluorinated group, which may contain one or more ether linkages, and may be a group represented by the following general formula, for example.
-[CF (CF 3 ) OCF 2 ] m (Rf) n-
Rf: linear or branched perfluoroalkylene group having 1 to 10 carbon atoms, preferably 1 to 4 carbon atoms
m: 0, 1 or 2
n: 0 or 1
[0008]
Examples of such dicarboxylic acid fluorides include the following compounds.
FOCCF (CF 3 ) OCF 2 COF
FOCCF (CF 3 ) O (CF 2 ) 2 COF
FOCCF (CF 3 ) O (CF 2 ) 3 COF
FOCCF (CF 3 ) O (CF 2 ) 4 COF
FOCCF (CF 3 ) O (CF 2 ) 5 COF
FOCCF (CF 3 ) OCF 2 CF (CF 3 ) OCF 2 COF
FOCCF (CF 3 ) OCF 2 CF (CF 3 ) O (CF 2 ) 2 COF
FOCCF (CF 3 ) OCF 2 CF (CF 3 ) O (CF 2 ) 3 COF
FOCCF (CF 3 ) OCF 2 CF (CF 3 ) O (CF 2 ) 4 COF
FOCCF (CF 3 ) OCF 2 CF (CF 3 ) O (CF 2 ) 5 COF
[0009]
Examples of alcohols that react with these dicarboxylic acid fluorides include alcohols having 3 or more carbon atoms such as propanol, isopropanol, n-butanol, isobutanol (2-butanol), 2-methyl-1-propanol, 4-heptanol, 2, 2-dimethyl-1-propanol, 2,4-dimethyl-3-pentanol and the like are used, and alcohol having a branching group is preferably used.
[0010]
The reaction between the two is carried out at a reaction temperature of about -60 to 60 ° C. using 0.7 to 2 mol, preferably about 1 to 1.5 mol, of alcohol with respect to 1 mol of dicarboxylic acid fluoride. The selectivity is improved when the reaction temperature is lower, but the reaction is preferably carried out at about -40 to 20 ° C. in view of the capacity and economics of the cooling device.
[0011]
This reaction can be carried out in the presence or absence of a solvent. When a solvent is used, any one can be used as long as the reaction is not inhibited, but diglyme used also in the synthesis step of dicarboxylic acid fluoride. Tetraglyme and the like are preferably used. Incidentally, hydrogen fluoride produced as a by-product of the condensation reaction is adsorbed by an alkali metal fluoride such as sodium fluoride coexisting in the reaction system, whereby corrosion of the reactor can be suppressed.
[0012]
【The invention's effect】
A copolymer obtained by copolymerizing perfluorovinyl ether is effectively used as a functional fluorine-containing polymer in applications such as water and oil repellents, but it is an intermediate for synthesizing perfluorovinyl ether as a component of such a copolymer. Monocarboxylic acid monoester fluoride FOCCF (CF 3 ) OCF 2 (A) p (CF 2 ) qCOOR of dicarboxylic acid having a perfluoroether bond as an ester, in the present invention, an alcohol having 3 or more carbon atoms is selected as an esterifying agent By using it, it can manufacture with a conversion rate and a favorable selectivity.
[0013]
【Example】
Next, the present invention will be described with reference to examples.
[0014]
Reference Example 327 g (1.1 mol) of perfluoroadipic acid fluoride, 15.2 g (0.1 mol) of cesium fluoride and 300 ml of diglyme were reacted with 199.2 g (1.2 mol) of hexafluoropropene oxide at 0 to 5 ° C. Dicarboxylic acid fluoride FOCCF (CF 3 ) O (CF 2 ) 5 COF was obtained by distillation.
[0015]
Example 1
In a glass reaction vessel with a capacity of 500 ml, charge 300 g (0.65 mol) of FOCCF (CF 3 ) O (CF 2 ) 5 COF and 33 g of sodium fluoride and stir while maintaining the internal temperature at -30 to -20 ° C. Then, 42.9 g (0.72 mol) of propanol was added dropwise over 2 hours. After completion of the dropwise addition, sodium fluoride was filtered off to obtain 287 g of a mixture of raw material 15.8%, monoester 48.5% and diester 35.7% by gas chromatography composition. The reaction conversion was 84.2%, the monoester selectivity was 57.6%, and the yield was 42.8%.
[0016]
Example 2
In Example 1, the same amount of isopropanol was used instead of propanol to obtain 285 g of a mixture of raw material 11.4%, monoester 59.1% and diester 25.6%. The conversion of the reaction was 88.6%, the monoester selectivity was 69.8%, and the yield was 51.8%.
[0017]
Example 3
In Example 1, instead of propanol, 63.3 g (0.72 mol) of 2,2-dimethyl-1-propanol was dissolved in 30 g of tetraglyme, and a mixture of raw material 6.8%, monoester 74.0% and diester 17.0% 328 g was obtained. The conversion of the reaction was 93.2%, the monoester selectivity was 81.3%, and the yield was 64.3%.
[0018]
Example 4
In Example 1, 234 g (0.65 mol) of FOCCF (CF 3 ) O (CF 2 ) 3 COF was used as the dicarboxylic acid fluoride, and 83.5 g (0.72 mol) of 2,4-dimethyl-3-pentanol was used instead of propanol. Was used to obtain 256 g of a mixture of raw material 5.8%, monoester 78.4% and diester 15.8%. The conversion of the reaction was 94.2%, the monoester selectivity was 83.2%, and the yield was 67.7%.
[0019]
Example 5
In Example 1, FOCCF (CF 3 ) O (CF 2 ) 2 COF 202 g (0.65 mol) was used as the dicarboxylic acid fluoride, and 83.5 g (0.72 mol) of 2,4-dimethyl-3-pentanol was used instead of propanol. Was used to obtain 220 g of a mixture of raw material 6.7%, monoester 76.6% and diester 16.7%. The reaction conversion was 93.3%, the monoester selectivity was 82.1%, and the yield was 63.9%.
[0020]
Comparative Example In Example 1, 22.9 g (0.72 mol) of methanol was used instead of propanol to obtain 262 g of a mixture of raw material 19.0%, monoester 42.9% and diester 38.1%. The conversion of the reaction was 81.0%, the monoester selectivity was 53.0%, and the yield was 36.6%.

Claims (3)

一般式
FOCCF(CF3)OCF2(A)p(CF2)qCOF
(ここで、Aは炭素数1〜10の二官能性パーフルオロ化基であり、pは0または1であり、そしてqは0または1〜10の整数である)で表わされる非対称ジカルボン酸フロライドを、炭素数3以上のアルコールと反応させ、 CF 2 COF 基側をエステル化させることを特徴とするジカルボン酸のモノエステルモノ酸フロライドの製造法。
General formula
FOCCF (CF 3 ) OCF 2 (A) p (CF 2 ) qCOF
(Wherein A is a bifunctional perfluorinated group having 1 to 10 carbon atoms, p is 0 or 1, and q is 0 or an integer of 1 to 10). Is reacted with an alcohol having 3 or more carbon atoms to esterify the CF 2 COF group, and a method for producing a monoester monoacid fluoride of a dicarboxylic acid.
非対称ジカルボン酸フロライドを表わす一般式中のA基が、一般式
-[CF(CF3)OCF2]m(Rf)n-
(ここで、Rfは炭素数1〜10のパーフルオロアルキレン基であり、mは0,1または2であり、そしてnは0または1である)で表わされる2価の基であるジカルボン酸フロライドが用いられた請求項1記載のジカルボン酸のモノエステルモノフロライドの製造法。
The A group in the general formula representing the asymmetric dicarboxylic acid fluoride is represented by the general formula
-[CF (CF 3 ) OCF 2 ] m (Rf) n-
(Wherein Rf is a perfluoroalkylene group having 1 to 10 carbon atoms, m is 0, 1 or 2, and n is 0 or 1). The method for producing a monoester monofluoride of dicarboxylic acid according to claim 1, wherein
炭素数3以上のアルコールが分岐基を有するアルコールである請求項1または2記載のジカルボン酸のモノエステルモノ酸フロライドの製造法。The method for producing a monoester monoacid fluoride of a dicarboxylic acid according to claim 1 or 2, wherein the alcohol having 3 or more carbon atoms is an alcohol having a branched group.
JP31320499A 1999-11-04 1999-11-04 Production method of monoester from dicarboxylic acid fluoride Expired - Fee Related JP4362908B2 (en)

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US09/699,656 US6407282B1 (en) 1999-11-04 2000-10-30 Process for producing monoester from dicarboxylic acid fluoride

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