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WO2007020816A1 - Process for producing difluoroacetic acid salt - Google Patents

Process for producing difluoroacetic acid salt Download PDF

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Publication number
WO2007020816A1
WO2007020816A1 PCT/JP2006/315484 JP2006315484W WO2007020816A1 WO 2007020816 A1 WO2007020816 A1 WO 2007020816A1 JP 2006315484 W JP2006315484 W JP 2006315484W WO 2007020816 A1 WO2007020816 A1 WO 2007020816A1
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Prior art keywords
hydroxide
potassium
metal
tetrafluoroethane
difluoroacetate
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French (fr)
Japanese (ja)
Inventor
Satoru Okamoto
Satoshi Yoshikawa
Yasuo Hibino
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Central Glass Co Ltd
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Central Glass Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/16Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
    • C07C51/295Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with inorganic bases, e.g. by alkali fusion

Definitions

  • the present invention relates to a method for producing difluoroacetate useful as an intermediate for medical and agricultural chemicals and an intermediate for functional materials.
  • a method for producing acetate a method of reacting acetic acid with a metal hydroxide has been widely known.
  • difluoroacetic acid is conventionally known as in the case of an acetate without a fluorine atom.
  • it is produced by reacting a metal hydroxide with a metal hydroxide, and examples other than this method have been known.
  • a method for producing difluoroacetic acid for example, in Patent Document 1, dichloroacetic acid chloride is reacted with a secondary amine to form N, N disubstituted dichloroacetic acid amide, and the N, N disubstituted dichloroacetic acid is produced.
  • a method for producing difluoroacetic acid by reacting an amide with a fluorinating agent such as an alkyl metal fluoride to form an N, N disubstituted difluoroacetamide, and then hydrolyzing the N, N disubstituted difluoroacetamide. ing.
  • Patent Document 2 S-difluoro-2-troethane is hydrolyzed in water to obtain difluoroacetic acid S.
  • Non-Patent Document 1 dichloroacetic acid methyl ester is converted to a fluoride such as KF.
  • a method for producing difluoroacetic acid by hydrolyzing methyl fluoroacetate after fluorination with difluoroacetic acid methyl ester is disclosed.
  • Patent Document 3 and Non-Patent Documents are disclosed as conventional techniques related to the present invention using 1 alkoxy 1,1,2,2-tetrafluoroethane represented by the formula [1] which is a raw material of the present invention.
  • Reference 2 [This is a 1-no-recoxi 1, 1, 2, 2--Terrafnore old Roetan, Anolemina (AI O)
  • R is an alkyl group having 1 to 4 carbon atoms.
  • Patent Document 1 JP-A-6-228043
  • Patent Document 2 JP-A-60-041634
  • Patent Document 3 JP-A-8-92162
  • Non-patent literature l Rec. Trav. Chim., 65 ⁇ , 427, 1947
  • Non-Patent Document 2 Reports Res. Lab. Asahi Glass Co., ltd., Vol. 47, 69-79, 1997
  • the method power S of reacting the corresponding difluoroacetic acid and metal hydroxide is considered to be the most common, but at that time, it is the raw material.
  • Method power to obtain difluoroacetic acid was not always easy.
  • a fluorinating agent that is difficult to handle must be used, and in addition, a large amount of waste such as inorganic salts after the reaction is by-produced.
  • multiple steps were taken to obtain difluoroacetic acid this was not advantageous for large-scale production.
  • sulfuric acid is used for hydrolysis, there is a problem that a large amount of sulfuric acid waste liquid is generated.
  • the above production method for obtaining difluoroacetate is difficult to produce difluoroacetate as a raw material, and a method for producing difluoroacetate by a more advantageous and efficient method is required. It was.
  • HCF 2 CF 2 OR 1 (Wherein R 1 represents a linear or branched alkyl group having 1 to 20 carbon atoms) and a difluoroacetate salt by reacting with an alcohol having 1 to 20 carbon atoms and a metal hydroxide or metal alkoxide.
  • R 1 represents a linear or branched alkyl group having 1 to 20 carbon atoms
  • R 1 represents a linear or branched alkyl group having 1 to 20 carbon atoms
  • a difluoroacetate salt by reacting with an alcohol having 1 to 20 carbon atoms and a metal hydroxide or metal alkoxide.
  • 1-alkoxy-1, 1, 2, 2-tetrafluoroethane which is a raw material of the present invention, has a fluorine atom as a carbon atom. Due to the strong electron withdrawing property of the fluorine atom, the reactivity of the hydrogen atom bonded to the ⁇ -position carbon atom becomes more energetically unstable than that without the fluorine atom, and the alkoxyalkane has been conventionally used. Unlike the complex substrate, it was expected that it would be extremely difficult to produce the corresponding difluoroacetate salt, which has a greater tendency to induce side reactions.
  • the present invention does not require the production of difluoroacetic acid, and is one-step from 1alkoxy 1,1,2,2-tetrafluoroethane and also includes waste.
  • the target difluoroacetate can be produced with a low and high selectivity. This is a particularly useful method for implementation on an industrial scale.
  • 1 alkoxy 1, 1, 2, 2-tetrafluoroethane represented by the formula [1] is reacted with an alcohol having 1 to 20 carbon atoms and a metal hydroxide or metal alkoxide.
  • a method for producing a metal salt of difluoroacetic acid is provided.
  • R 1 in the 1 alkoxy 1, 1, 2, 2-tetrafluoroethane represented by the formula [1] used in this reaction represents a linear or branched alkyl group having 1 to 20 carbon atoms.
  • 1S the usefulness of the linear or branched alkyl group strength product having 1 to 10 carbon atoms and the effect of coexistence are particularly remarkable, more preferably 1 to 6 carbon atoms. Or a linear or branched alkyl group.
  • 1-methoxy 1, 1, 2, 2-tetrafluoroethanethane (HFE-254pc) which is relatively easy to produce, is preferred!
  • Examples of the alcohol having 1 to 20 carbon atoms used in the present invention include an alcohol represented by ROH, and R represents a linear, branched or cyclic alkyl group having 1 to 20 carbon atoms. (Wherein some or all of the hydrogen atoms may be replaced by halogen (fluorine, chlorine, bromine, iodine)) or aryl groups (where some or all of the hydrogen atoms are halogen (fluorine, Chlorine, bromine, iodine).
  • methanol, ethanol, n— Propanol, n-butanol Preferably methanol, ethanol, n— Propanol, n-butanol.
  • the metal hydroxide is not particularly limited as long as it is a metal hydroxide that allows the reaction to proceed efficiently.
  • Group power consisting of potassium hydroxide, sodium hydroxide, lithium hydroxide, calcium hydroxide, magnesium hydroxide, and calcium hydroxide. At least one selected from the group is preferred. Particularly preferred.
  • the metal alkoxide is selected from the group consisting of sodium methoxide, potassium methoxide, sodium ethoxide, potassium ethoxide, sodium n-propoxide, potassium n-propoxide, sodium isopropoxide, potassium isopropoxide.
  • potassium methoxide is selected from the group consisting of sodium methoxide, potassium methoxide, sodium ethoxide, potassium ethoxide, sodium n-propoxide, potassium n-propoxide, sodium isopropoxide, potassium isopropoxide.
  • potassium methoxide is particularly preferred.
  • the reaction of the present invention comprises diphloor metal acetate by reacting 1-alkoxy 1, 1, 2, 2-tetrafluoroethane with an alcohol having 1 to 20 carbon atoms and a metal hydroxide. Although it is a manufacturing method of salt, if a preferable combination is shown, it will be represented by the following reaction formula.
  • one alkoxy 1,1,2,2-tetrafluoroethane has 1 mol of alcohol per 1 mol. Alcohol is charged excessively and the cost is high. It is industrially useful to adjust the consumption of 2,2-tetrafluoroethane to increase.
  • the molar ratio of 1 alkoxy 1,1,2,2-tetrafluoroethane and alcohol is 1: 0.5-1: 200, preferably 1: 1-1: 100, more preferably Can be added from 1: 1 to L: 20 and metal hydroxide and 1alkoxy 1,1,2,2-tetrafluoroethane consumed as the reaction proceeds.
  • alcohol is used as a reaction reagent, and since it can function as a solvent, it is not usually necessary to use another solvent.
  • a solvent The reaction rate can be increased by adding an aprotic polar solvent into the reaction system.
  • the aprotic polar solvent used in this reaction is not particularly limited, but dimethyl sulfoxide (DMSO), dimethylacetamide (DMAC), dimethylformamide (D MF), nitromethane, acetonitrile, hexamethylphosphoric triamide (HMPA), glyme, diglyme, jetyl ether, tetrahydrofuran (THF), 1,4 dioxane, etc.
  • DMSO dimethyl sulfoxide
  • DMAC dimethylacetamide
  • DMF dimethylformamide
  • HMPA hexamethylphosphoric triamide
  • glyme diglyme, jetyl ether, tetrahydrofuran (THF), 1,4 dioxane, etc.
  • the amount of the solvent used is usually 0.05 to 1 times mol, preferably 0.1 to 0.3 times mol for 1 mol of 1 alkoxy 1,1,2,2-tetrafluoroethane. It is appropriately selected from the range.
  • Metal hydroxide or metal alkoxide for example, in KOH stoichiometrically added to an excess of force to react 3 moles per mole of 1 alkoxy 1, 1, 2, 2-tetrafluoroethane. If the reaction system! Since there is an increased possibility that the metal salt of difluoroacetic acid that is produced and precipitated will be precipitated together with the metal hydroxide or metal alkoxide, it becomes difficult to purify it.
  • the reaction pressure is not particularly limited, the reaction pressure is 0.1 lMPa to l. OMPa (absolute pressure, hereinafter the same in the present specification), and preferably 0.1 lMPa to 0.6 MPa. It is.
  • the target metal salt of difluoroacetate can be produced even under a mild pressure condition of 0.1 MPa to 0.6 MPa.
  • reaction temperature is not particularly limited, it can be carried out under relatively mild temperature conditions, and is in the range of 0 ° C to 100 ° C, preferably 20 ° C to 80 ° C, more preferably 30 °. C ⁇ 70 ° C is good. If the reaction temperature is too low, the reaction does not proceed, and if it is too high, the probability of side reactions increases, which is not economically preferable.
  • This reaction is a semi-continuous method in which a liquid alcohol in which a metal hydroxide is saturated into 1 alkoxy 1, 1, 2, 2-tetrafluoroethane is continuously introduced, metal hydroxide.
  • a semi-continuous system in which 1 alkoxy 1, 1, 2, 2-tetrafluoroethane is continuously introduced into liquid alcohol saturated with the product, or a batch in which all raw materials are charged into the reactor at once. It does not specifically limit, such as performing by a formula. Also, it can be produced in a continuous system in which a metal hydroxide saturated alcohol and 1-alkoxy 1,1,2,2-tetrafluoroethane are introduced into the reactor and the product is continuously withdrawn. .
  • the reactor is a material having heat resistance and corrosion resistance to fluorine, hydrogen fluoride, hydrogen chloride, etc.
  • 1 alkoxy 1, 1, 2, 2-tetrafluoroethane represented by the formula [1] in this reaction has a low boiling point (50 ° C or less) under normal temperature and atmospheric pressure conditions, so the reaction temperature If it is high, it may vaporize.
  • a pressure-resistant reaction vessel is used, and the vessel can be sealed and the reaction can be carried out by the batch method described above under the conditions of the pressure described above.
  • the method for the purification treatment of difluoroacetic acid metal salt is not particularly limited.
  • the resulting difluoroacetate salt has a lower solubility in 1-alkoxy 1, 1, 2, 2-tetrafluoroethane represented by the formula [1].
  • the reaction solution it precipitates with KF as an insoluble solid mixture.
  • the solid mixture can be easily separated by combining ordinary filtration operations.
  • To isolate difluoroacetic acid metal salt from the solid mixture use the difference in solubility with KF and dissolve in a good solvent such as methanol or ethanol, and add a poor solvent such as ether or hexane. It can be analyzed and separated.
  • the difluoroacetate can also be converted to difluoroacetic acid by reaction with an acid such as hydrochloric acid or sulfuric acid.
  • the difluoroacetate is then converted into difluoroacetic acid and the mixture solution power is extracted with a solvent such as ether, and then It can be separated by a normal distillation operation.
  • 1alkoxy 1,1,2,2-tetrafluoroethane as a starting material of the present invention can be produced by a known method. For example, a predetermined amount of methanol and a metal hydroxide are added to a pressure reactor. 1) After introducing a certain amount of tetrafluoroethylene (TFE) to form 1 alkoxy 1, 1, 2, 2-tetrafluoroethane, the reaction proceeds with the method of the present invention. It is also possible to produce a difluoroacetic acid metal salt.
  • TFE tetrafluoroethylene
  • the difluoroacetic acid metal salt obtained by the present invention is a very useful compound used as an intermediate for medical and agricultural chemicals and an intermediate for functional materials.
  • the obtained difluoroacetic acid metal salt can be easily converted to difluoroacetic acid by an acid hydrolysis reaction such as hydrochloric acid or sulfuric acid.
  • Example 1 The power to specifically describe the present invention with reference to examples below. The present invention is not limited by these. Example 1

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

A process for producing a metal difluoroacetate which comprises reacting a 1-alkoxy-1,1,2,2-tetrafluoroethane represented by the formula [1]: [Chemical formula 4] HCF2 CF2 OR1 (1) (wherein R1 represents C1-20 linear or branched alkyl) with a C1-20 alcohol and either a metal hydroxide or a metal alkoxide.

Description

明 細 書  Specification

ジフルォロ酢酸塩の製造方法  Method for producing difluoroacetate

技術分野  Technical field

[0001] 本発明は、医農薬の中間体および機能性材料の中間体等として有用なジフルォロ 酢酸塩の製造方法に関する。  TECHNICAL FIELD [0001] The present invention relates to a method for producing difluoroacetate useful as an intermediate for medical and agricultural chemicals and an intermediate for functional materials.

発明の背景  Background of the Invention

[0002] 酢酸塩の製造方法として、酢酸と金属水酸化物を反応させる方法が従来から広く知 られている。一方、フッ素原子を持つ酢酸塩、例えば、本発明の対象となるジフルォ 口酢酸塩の製造法に関しては、従来から知られて 、るフッ素原子のな 、酢酸塩の製 造方法と同様、ジフルォロ酢酸と金属水酸化物を反応させて製造しているのが一般 的であり、この方法以外に製造する例は知られていな力つた。  [0002] As a method for producing acetate, a method of reacting acetic acid with a metal hydroxide has been widely known. On the other hand, with respect to a method for producing an acetate having a fluorine atom, for example, a difluoroacetate which is a subject of the present invention, difluoroacetic acid is conventionally known as in the case of an acetate without a fluorine atom. In general, it is produced by reacting a metal hydroxide with a metal hydroxide, and examples other than this method have been known.

[0003] ここで、ジフルォロ酢酸の製造方法として、例えば特許文献 1では、ジクロロ酢酸クロ リドを 2級ァミンと反応させて N, N ジ置換ジクロ口酢酸アミドとし、該 N, N ジ置換 ジクロロ酢酸アミドをアルキル金属フッ素化物等のフッ素化剤と反応させて N, N ジ 置換ジフルォロ酢酸アミドとした後に、該 N, N ジ置換ジフルォロ酢酸アミドを加水 分解してジフルォロ酢酸を製造する方法が開示されている。  Here, as a method for producing difluoroacetic acid, for example, in Patent Document 1, dichloroacetic acid chloride is reacted with a secondary amine to form N, N disubstituted dichloroacetic acid amide, and the N, N disubstituted dichloroacetic acid is produced. Disclosed is a method for producing difluoroacetic acid by reacting an amide with a fluorinating agent such as an alkyl metal fluoride to form an N, N disubstituted difluoroacetamide, and then hydrolyzing the N, N disubstituted difluoroacetamide. ing.

[0004] また、特許文献 2では、 1, 1ージフルオロー 2 -トロエタンをカ卩水分解してジフル ォロ酢酸を得る方法力 S、非特許文献 1ではジクロロ酢酸メチルエステルを KFなどのフ ッ化物でフッ素化してジフルォロ酢酸メチルエステルとした後、フルォロ酢酸メチルェ ステルを加水分解してジフルォロ酢酸を得る製造方法が開示されて 、る。  [0004] In Patent Document 2, 1, S-difluoro-2-troethane is hydrolyzed in water to obtain difluoroacetic acid S. In Non-Patent Document 1, dichloroacetic acid methyl ester is converted to a fluoride such as KF. And a method for producing difluoroacetic acid by hydrolyzing methyl fluoroacetate after fluorination with difluoroacetic acid methyl ester is disclosed.

[0005] 一方、本発明の原料である式 [1]で表される 1 アルコキシ 1, 1, 2, 2—テトラフ ルォロェタンを用いた、本発明と関連する従来技術として、特許文献 3や非特許文献 2【こお!ヽて、 1ーァノレコキシ 1, 1, 2, 2—テ卜ラフノレ才ロェタンを、ァノレミナ(AI O )  [0005] On the other hand, Patent Document 3 and Non-Patent Documents are disclosed as conventional techniques related to the present invention using 1 alkoxy 1,1,2,2-tetrafluoroethane represented by the formula [1] which is a raw material of the present invention. Reference 2 [This is a 1-no-recoxi 1, 1, 2, 2--Terrafnore old Roetan, Anolemina (AI O)

2 3 等の金属酸化物触媒の存在下に気相反応させてジフルォロ酢酸フルオリド (HCF C  Gas phase reaction in the presence of a metal oxide catalyst such as 2 3

2 2

OF)とし、さらにアルコール類とを反応させてジフルォロ酢酸エステル(HCF COOR OF) and further reacting with alcohols to produce difluoroacetic acid ester (HCF COOR

2 2

。 Rは炭素数 1〜4のアルキル基)とする方法が開示されている。 . A method in which R is an alkyl group having 1 to 4 carbon atoms is disclosed.

特許文献 1:特開平 6 - 228043号 特許文献 2:特開昭 60— 041634号公報 Patent Document 1: JP-A-6-228043 Patent Document 2: JP-A-60-041634

特許文献 3 :特開平 8— 92162号  Patent Document 3: JP-A-8-92162

非特許文献 l :Rec. Trav. chim. , 65卷、 427, 1947年  Non-patent literature l: Rec. Trav. Chim., 65 卷, 427, 1947

非特許文献 2 : Reports Res. Lab. Asahi Glass Co. , ltd. , Vol. 47、 69— 79 頁、 1997年  Non-Patent Document 2: Reports Res. Lab. Asahi Glass Co., ltd., Vol. 47, 69-79, 1997

発明の概要  Summary of the Invention

[0006] ジフルォロ酢酸塩を製造する方法として、前述したように対応するジフルォロ酢酸と 金属水酸ィ匕物を反応させる方法力 Sもっとも一般的であると考えられるが、その際、原 料であるジフルォロ酢酸を得る方法力 必ずしも容易なものではな力つた。例えば、 特許文献 1の方法では、取扱いが困難なフッ素化剤を使用しなくてはならず、その上 、反応後の無機塩等の廃棄物が多く副生する。更にジフルォロ酢酸を得るために複 数の工程を経ることから、大規模での製造には有利とは言えなカゝつた。特許文献 2の 方法では、加水分解に硫酸を使用する為、大量の硫酸廃液を生じる問題がある。特 許文献 3や非特許文献 2の方法では、本発明の原料である式 [1]で表される 1 アル コキシ—1, 1, 2, 2—テトラフルォロェタンを、金属酸ィ匕物触媒を用いて気相反応さ せ、いったん別の化合物に誘導しなくてはならず、さらに特許文献 3や非特許文献 1 、そして非特許文献 2ではジフルォロ酢酸塩を得るために、ジフルォロ酢酸エステル を更に加水分解してジフルォロ酢酸を得た後に、金属水酸化物を反応させなくては ならないなど、多段階の工程が必要であった。  [0006] As described above, as a method for producing difluoroacetate, the method power S of reacting the corresponding difluoroacetic acid and metal hydroxide is considered to be the most common, but at that time, it is the raw material. Method power to obtain difluoroacetic acid was not always easy. For example, in the method of Patent Document 1, a fluorinating agent that is difficult to handle must be used, and in addition, a large amount of waste such as inorganic salts after the reaction is by-produced. Furthermore, since multiple steps were taken to obtain difluoroacetic acid, this was not advantageous for large-scale production. In the method of Patent Document 2, since sulfuric acid is used for hydrolysis, there is a problem that a large amount of sulfuric acid waste liquid is generated. In the methods of Patent Document 3 and Non-Patent Document 2, 1-alkoxy-1, 1, 2, 2-tetrafluoroethane represented by the formula [1], which is a raw material of the present invention, is converted into a metal oxide. In order to obtain difluoroacetate in Patent Document 3, Non-Patent Document 1, and Non-Patent Document 2, it is necessary to conduct a gas phase reaction using a physical catalyst and to derive once to another compound. After further hydrolysis of the ester to obtain difluoroacetic acid, a multi-step process was required, for example, the metal hydroxide had to be reacted.

[0007] このように、ジフルォロ酢酸塩を得るための上記製造方法は、原料であるジフルォロ 酢酸の生産が困難であり、より有利かつ効率的な方法で、ジフルォロ酢酸塩を製造 する方法が求められていた。  As described above, the above production method for obtaining difluoroacetate is difficult to produce difluoroacetate as a raw material, and a method for producing difluoroacetate by a more advantageous and efficient method is required. It was.

[0008] 本発明者らは、鋭意検討を重ねた結果、式 [1]で表される 1 アルコキシ 1, 1, 2 , 2—テトラフルォロェタン  [0008] As a result of intensive studies, the present inventors have found that 1 alkoxy 1, 1, 2, 2-tetrafluoroethane represented by the formula [1]

[化 1]  [Chemical 1]

H C F2 C F2 OR1 (ただし、 R1 は炭素数 1〜20の直鎖または分岐鎖のアルキル基を示す。)を、炭素 数 1〜20のアルコールおよび、金属水酸化物もしくは金属アルコキシドと反応させる ことによりジフルォロ酢酸塩が製造できることを見出し、本発明に達した。 HCF 2 CF 2 OR 1 (Wherein R 1 represents a linear or branched alkyl group having 1 to 20 carbon atoms) and a difluoroacetate salt by reacting with an alcohol having 1 to 20 carbon atoms and a metal hydroxide or metal alkoxide. The present invention has been found.

[0009] これまでに、フッ素原子を持たない、アルコキシアルカン化合物に対して、本発明と 同様に対応する酢酸塩を製造する技術は知られていなカゝつた。例えば、 1—アルコ キシェタンに対して、炭素数 1〜20のアルコールおよび、金属水酸化物もしくは金属 アルコキシドを反応させても、反応は進行せず、対応する酢酸塩は全く得られない( 比較例 1を参照)。 [0009] To date, a technique for producing a corresponding acetate salt of an alkoxyalkane compound having no fluorine atom in the same manner as in the present invention has not been known. For example, even if 1-alcoxetane is reacted with an alcohol having 1 to 20 carbon atoms and a metal hydroxide or metal alkoxide, the reaction does not proceed and no corresponding acetate is obtained (Comparative Example) (See 1).

[0010] 一方、本発明の原料である 1—アルコキシ—1, 1, 2, 2—テトラフルォロェタンは、炭 素原子にフッ素原子が存在する。このフッ素原子の強い電子求引性のため、 α位の 炭素原子に結合している水素原子の反応性は、フッ素原子を持たないそれと比べて 、さらにエネルギー的に不安定となり、従来、アルコキシアルカンィ匕合物の基質とは 異なり、副反応を誘発する傾向も大きぐ対応するジフルォロ酢酸塩を製造するのは 極めて困難であると予想された。  [0010] On the other hand, 1-alkoxy-1, 1, 2, 2-tetrafluoroethane, which is a raw material of the present invention, has a fluorine atom as a carbon atom. Due to the strong electron withdrawing property of the fluorine atom, the reactivity of the hydrogen atom bonded to the α-position carbon atom becomes more energetically unstable than that without the fluorine atom, and the alkoxyalkane has been conventionally used. Unlike the complex substrate, it was expected that it would be extremely difficult to produce the corresponding difluoroacetate salt, which has a greater tendency to induce side reactions.

[0011] ところが発明者らは、このようなフッ素原子を持つ反応基質にアルコール及び金属水 酸化物等を反応させたところ、副生成物がまったく得られず、目的とするジフルォロ 酢酸塩を容易に製造できると!ヽぅ知見を得た。  However, the inventors reacted alcohol and metal hydroxide with a reaction substrate having such a fluorine atom, so that no by-product was obtained at all, and the intended difluoroacetate was easily obtained. When it could be manufactured, I got knowledge.

[0012] 前述の従来公知の方法と比べ、本発明では、ジフルォロ酢酸の製造を必要とせず、 さらに 1 アルコキシ 1, 1, 2, 2—テトラフルォロェタンから一段階で、かつ廃棄物 も少なく高選択率にて該目的物であるジフルォロ酢酸塩を製造できる。工業規模で 実施する上で、特に有用な方法である。  [0012] Compared with the above-mentioned conventionally known methods, the present invention does not require the production of difluoroacetic acid, and is one-step from 1alkoxy 1,1,2,2-tetrafluoroethane and also includes waste. The target difluoroacetate can be produced with a low and high selectivity. This is a particularly useful method for implementation on an industrial scale.

[0013] 本発明に依れば、式 [1]で表される 1 アルコキシ 1, 1, 2, 2—テトラフルォロェ タンを炭素数 1〜20のアルコールおよび、金属水酸化物もしくは金属アルコキシドと 反応させることを含む、ジフルォロ酢酸金属塩の製造方法が提供される。  [0013] According to the present invention, 1 alkoxy 1, 1, 2, 2-tetrafluoroethane represented by the formula [1] is reacted with an alcohol having 1 to 20 carbon atoms and a metal hydroxide or metal alkoxide. A method for producing a metal salt of difluoroacetic acid is provided.

詳細な説明  Detailed description

[0014] 入手容易な医農薬の中間体および機能性材料の中間体等として有用なジフルォ 口酢酸塩を、上述の従来技術と異なり、安価な材料を用い、一段階で効率よくかつェ 業的に製造することが可能となった。 [0015] 本発明の原料である式 [1]で表される 1 アルコキシ 1, 1, 2, 2—テトラフルォロ エタンは、公知の化合物であり、対応するアルコール化合物(R1 OH)とテトラフルォ 口エチレンとを塩基の存在下に反応させる方法で合成できる (J. Am. Chem. Soc. , 73, 1329 (1951) )。 [0014] Difluoacetate, which is useful as an intermediate for readily available medicines and agrochemicals and an intermediate for functional materials, is different from the above-mentioned conventional technology, uses inexpensive materials, and is efficient and technical in one step. It became possible to manufacture. 1 Alkoxy 1, 1, 2, 2-tetrafluoroethane represented by the formula [1] as a raw material of the present invention is a known compound, and the corresponding alcohol compound (R 1 OH) and tetrafluoroethylene Can be synthesized in the presence of a base (J. Am. Chem. Soc., 73, 1329 (1951)).

[0016] 本反応で用いられる式 [1]で表される 1 アルコキシ 1, 1, 2, 2—テトラフルォロ ェタンにおける R1としては、炭素数 1〜20の直鎖または分岐鎖のアルキル基を示す 1S この中で、炭素数 1〜10の直鎖または分岐鎖のアルキル基力 生成物の有用性 や、共存させることの効果が特に顕著であることから好ましぐさらに好ましくは炭素数 1〜6の直鎖または分岐鎖のアルキル基である。具体的には、 1—メトキシ— 1, 1, 2 , 2—テトラフルォロェタン、 1 エトキシ 1, 1, 2, 2—テトラフルォロェタン、 l—(n プロポキシ) 1, 1, 2, 2—テトラフルォロェタン、 1 イソプロポキシ 1, 1, 2, 2 ーテトラフルォロェタン、 1ー(11ーブトキシ)ー1, 1, 2, 2—テトラフルォロェタン等が 挙げられるが、これらのなかで比較的製造が容易な 1ーメトキシ 1, 1, 2, 2—テトラ フルォロェタン(HFE - 254pc)が好まし!/ヽ。 [0016] R 1 in the 1 alkoxy 1, 1, 2, 2-tetrafluoroethane represented by the formula [1] used in this reaction represents a linear or branched alkyl group having 1 to 20 carbon atoms. 1S Among these, the usefulness of the linear or branched alkyl group strength product having 1 to 10 carbon atoms and the effect of coexistence are particularly remarkable, more preferably 1 to 6 carbon atoms. Or a linear or branched alkyl group. Specifically, 1-methoxy-1, 1, 2, 2-tetrafluoroethane, 1 ethoxy 1, 1, 2, 2-tetrafluoroethane, l- (n propoxy) 1, 1, 2 , 2-tetrafluoroethane, 1 isopropoxy 1, 1, 2, 2-tetrafluoroethane, 1- (11-butoxy) -1, 1, 2, 2-tetrafluoroethane, etc. Of these, 1-methoxy 1, 1, 2, 2-tetrafluoroethane (HFE-254pc), which is relatively easy to produce, is preferred!

[0017] 本発明で用いられる炭素数 1〜20のアルコールとしては、 ROHで表されるアルコー ルが挙げられ、 Rとしては、炭素数 1〜20の直鎖、分岐鎖、あるいは環状のアルキル 基 (ここで水素原子の一部または全てはハロゲン (フッ素、塩素、臭素、ヨウ素)で置 換されていても良い)、またはァリール基 (ここで水素原子の一部または全てはハロゲ ン (フッ素、塩素、臭素、ヨウ素)で置換されて良い)が挙げられる。  [0017] Examples of the alcohol having 1 to 20 carbon atoms used in the present invention include an alcohol represented by ROH, and R represents a linear, branched or cyclic alkyl group having 1 to 20 carbon atoms. (Wherein some or all of the hydrogen atoms may be replaced by halogen (fluorine, chlorine, bromine, iodine)) or aryl groups (where some or all of the hydrogen atoms are halogen (fluorine, Chlorine, bromine, iodine).

[0018] この中で、炭素数 1〜10の直鎖、分岐鎖、あるいは環状のアルコール力 生成物の 有用性や、共存させることの効果が特に顕著であることから好ましぐさらに好ましくは 炭素数 1〜6の直鎖、分岐鎖、あるいは環状のアルコールである。  [0018] Among these, the usefulness of a linear, branched or cyclic alcohol power product having 1 to 10 carbon atoms and the effect of coexistence are particularly remarkable. A linear, branched or cyclic alcohol having a number of 1 to 6.

[0019] 具体的には、例えばメタノール、エタノール、 n—プロパノール、イソプロパノール、 n ーブタノール、イソブタノール、 tーブタノール、 n—へキサノール、トリフルォロェタノ ール、へキサフルォロプロパノール、フエノール、ァ-ソール、メチルフエノール、 -ト 口フエノール、桂皮アルコール等を使用できる力 好ましくは、メタノール、エタノール 、 n 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、 sec ブタノ ール、 tert—ブタノール、フエノールが、さらに好ましくはメタノール、エタノール、 n— プロパノール、 n—ブタノールである。 Specifically, for example, methanol, ethanol, n-propanol, isopropanol, n-butanol, isobutanol, t-butanol, n-hexanol, trifluoroethanol, hexafluoropropanol, phenol, alcohol -Mole, ethanol, n-propanol, isopropanol, n-butanol, isobutanol, sec-butanol, tert-butanol, phenol, and more Preferably methanol, ethanol, n— Propanol, n-butanol.

[0020] 金属水酸化物としては、反応を効率的に進ませる金属水酸化物であれば特に限定 されない。水酸ィ匕カリウム、水酸化ナトリウム、水酸化リチウム、水酸ィ匕セシウム、水酸 ィ匕マグネシウム、水酸ィ匕カルシウムよりなる群力 選ばれる少なくとも 1種が好ましぐ 水酸ィ匕カリウムが特に好ましい。  [0020] The metal hydroxide is not particularly limited as long as it is a metal hydroxide that allows the reaction to proceed efficiently. Group power consisting of potassium hydroxide, sodium hydroxide, lithium hydroxide, calcium hydroxide, magnesium hydroxide, and calcium hydroxide. At least one selected from the group is preferred. Particularly preferred.

[0021] 金属アルコキシドとしては、ナトリウムメトキシド、カリウムメトキシド、ナトリウムエトキシ ド、カリウムエトキシド、ナトリウム n—プロポキシド、カリウム n—プロポキシド、ナトリウム イソプロボキシド、カリウムイソプロボキシドよりなる群力 選ばれる少なくとも 1種が好 ましぐカリウムメトキシドが特に好ましい。  [0021] The metal alkoxide is selected from the group consisting of sodium methoxide, potassium methoxide, sodium ethoxide, potassium ethoxide, sodium n-propoxide, potassium n-propoxide, sodium isopropoxide, potassium isopropoxide. One preferred is potassium methoxide, and particularly preferred.

[0022] 本発明の反応は、 1—アルコキシ 1, 1, 2, 2—テトラフルォロェタンと炭素数 1〜2 0のアルコールおよび金属水酸ィ匕物と反応させることによるジフォ口酢酸金属塩の製 造方法であるが、好ましい組合せを示せば、以下の反応式であらわされる。 [0022] The reaction of the present invention comprises diphloor metal acetate by reacting 1-alkoxy 1, 1, 2, 2-tetrafluoroethane with an alcohol having 1 to 20 carbon atoms and a metal hydroxide. Although it is a manufacturing method of salt, if a preferable combination is shown, it will be represented by the following reaction formula.

[化 2]  [Chemical 2]

HCF2CF2OCH3 + CH30H + 3K0H ~► CF2HC00K + CH3OCH3 + 2KF + 2H20 HCF 2 CF 2 OCH 3 + CH 3 0H + 3K0H ~ ► CF 2 HC00K + CH3OCH3 + 2KF + 2H 2 0

[0023] 本反応は 1 アルコキシ 1, 1, 2, 2—テトラフルォロェタン 1モルにつきアルコー ルは 1モル反応する力 アルコール量を過剰に仕込み、コスト的に高い 1 アルコキ シ 1, 1, 2, 2—テトラフルォロェタンの消費量が多くなるように調整するのが工業 的に有禾 ljである。 [0023] In this reaction, one alkoxy 1,1,2,2-tetrafluoroethane has 1 mol of alcohol per 1 mol. Alcohol is charged excessively and the cost is high. It is industrially useful to adjust the consumption of 2,2-tetrafluoroethane to increase.

[0024] 1 アルコキシ 1, 1, 2, 2—テトラフルォロェタン及びアルコールのモル比は、 1 : 0 . 5-1 : 200が用いられ、好ましくは 1: 1〜1: 100、さらに好ましくは 1: 1〜: L: 20で、 反応の進行とともに消費される金属水酸ィ匕物および 1 アルコキシ 1, 1, 2, 2—テ トラフルォロェタンを追加することができる。  [0024] The molar ratio of 1 alkoxy 1,1,2,2-tetrafluoroethane and alcohol is 1: 0.5-1: 200, preferably 1: 1-1: 100, more preferably Can be added from 1: 1 to L: 20 and metal hydroxide and 1alkoxy 1,1,2,2-tetrafluoroethane consumed as the reaction proceeds.

[0025] 本発明は、反応試剤としてアルコールを使用しており、これが溶媒としても機能でき ることから、通常は他の溶媒を使用する必要はないが、本発明においては、溶媒、中 でも、非プロトン性極性溶媒を反応系内に加えることで反応速度を上昇させることが できる。本反応で用いる非プロトン性極性溶媒としては、特に限定されないが、ジメチ ルスルホキシド(DMSO)、ジメチルァセトアミド(DMAC)、ジメチルホルムアミド(D MF)、ニトロメタン、ァセトニトリル、へキサメチルホスホリックトリアミド(HMPA)、グラ ィム、ジグライム、ジェチルエーテル、テトラヒドロフラン (THF)、 1, 4 ジォキサン等 の溶媒が挙げられる力 中でもジメチルスルホキシド(DMSO)、ジメチルァセトアミド (DMAC)、ジメチルホルムアミド(DMF)等を好適に用いることができる。 [0025] In the present invention, alcohol is used as a reaction reagent, and since it can function as a solvent, it is not usually necessary to use another solvent. However, in the present invention, a solvent, The reaction rate can be increased by adding an aprotic polar solvent into the reaction system. The aprotic polar solvent used in this reaction is not particularly limited, but dimethyl sulfoxide (DMSO), dimethylacetamide (DMAC), dimethylformamide (D MF), nitromethane, acetonitrile, hexamethylphosphoric triamide (HMPA), glyme, diglyme, jetyl ether, tetrahydrofuran (THF), 1,4 dioxane, etc. , Dimethylacetamide (DMAC), dimethylformamide (DMF) and the like can be preferably used.

[0026] 溶媒の使用量としては、 1 アルコキシ 1, 1, 2, 2—テトラフルォロェタン 1モルに 対して通常 0. 05〜1倍モル、好ましくは 0. 1〜0. 3倍モルの範囲から適宜選択され る。 [0026] The amount of the solvent used is usually 0.05 to 1 times mol, preferably 0.1 to 0.3 times mol for 1 mol of 1 alkoxy 1,1,2,2-tetrafluoroethane. It is appropriately selected from the range.

[0027] 金属水酸ィ匕物あるいは金属アルコキシドは、例えば KOHでは化学量論的には 1 アルコキシ 1, 1, 2, 2—テトラフルォロェタン 1モルにつき 3モル反応する力 過剰 に添加した場合反応系にお!ヽて生成、析出するジフルォロ酢酸金属塩が金属水酸 化物あるいは金属アルコキシドとともに析出する可能性が高まり、精製が困難になる ことから化学量論以上の添カ卩は特に必要ない。  [0027] Metal hydroxide or metal alkoxide, for example, in KOH stoichiometrically added to an excess of force to react 3 moles per mole of 1 alkoxy 1, 1, 2, 2-tetrafluoroethane. If the reaction system! Since there is an increased possibility that the metal salt of difluoroacetic acid that is produced and precipitated will be precipitated together with the metal hydroxide or metal alkoxide, it becomes difficult to purify it.

[0028] 反応圧力は特に限定されないが、反応圧力としては、 0. lMPa〜l. OMPa (絶対 圧。以下、本明細書にて同じ。)であり、好ましくは、 0. lMPa〜0. 6MPaである。本 発明においては、 0. lMPa〜0. 6MPaという温和な圧力条件でも目的とするジフル ォロ酢酸金属塩を製造することができる。  [0028] Although the reaction pressure is not particularly limited, the reaction pressure is 0.1 lMPa to l. OMPa (absolute pressure, hereinafter the same in the present specification), and preferably 0.1 lMPa to 0.6 MPa. It is. In the present invention, the target metal salt of difluoroacetate can be produced even under a mild pressure condition of 0.1 MPa to 0.6 MPa.

[0029] 反応温度は特に制限されないが、比較的穏和な温度条件で行うことができ、 0°C〜 100°Cの範囲であり、好ましくは 20°C〜80°C、更に好ましくは 30°C〜70°Cがよい。 反応温度が低すぎると反応が進行せず、高すぎると副反応の確率が高まるため、経 済的に好ましくない。  [0029] Although the reaction temperature is not particularly limited, it can be carried out under relatively mild temperature conditions, and is in the range of 0 ° C to 100 ° C, preferably 20 ° C to 80 ° C, more preferably 30 °. C ~ 70 ° C is good. If the reaction temperature is too low, the reaction does not proceed, and if it is too high, the probability of side reactions increases, which is not economically preferable.

[0030] 本反応は 1 アルコキシ 1, 1, 2, 2—テトラフルォロェタンに金属水酸ィ匕物を飽 和させた液体状のアルコールを連続的に導入する半連続方式、金属水酸化物を飽 和させた液体状のアルコールに 1 アルコキシ 1, 1, 2, 2—テトラフルォロェタン を連続的に導入する半連続方式、または全ての原料を一括して反応器に仕込むバ ツチ式で行う等、特に限定されない。また、金属水酸化物を飽和したアルコール及び 1—アルコキシ 1, 1, 2, 2—テトラフルォロエタンをともに反応器に導入し、生成物 を連続的に抜き出す連続式で製造することができる。  [0030] This reaction is a semi-continuous method in which a liquid alcohol in which a metal hydroxide is saturated into 1 alkoxy 1, 1, 2, 2-tetrafluoroethane is continuously introduced, metal hydroxide. A semi-continuous system in which 1 alkoxy 1, 1, 2, 2-tetrafluoroethane is continuously introduced into liquid alcohol saturated with the product, or a batch in which all raw materials are charged into the reactor at once. It does not specifically limit, such as performing by a formula. Also, it can be produced in a continuous system in which a metal hydroxide saturated alcohol and 1-alkoxy 1,1,2,2-tetrafluoroethane are introduced into the reactor and the product is continuously withdrawn. .

[0031] 反応器は、耐熱性とフッ素やフッ化水素、塩化水素等に対する耐食性を有する材質 で作られれば良ぐステンレス鋼、インコネル、ハステロイなどが好ましい。また、これら の金属でライニングされた材料で作ることもできる。 [0031] The reactor is a material having heat resistance and corrosion resistance to fluorine, hydrogen fluoride, hydrogen chloride, etc. Stainless steel, Inconel, Hastelloy, etc., which are good if made with, are preferable. It can also be made from materials lined with these metals.

[0032] また、本反応における式 [1]で表される 1 アルコキシ 1, 1, 2, 2—テトラフルォロ エタンは、常温、常圧条件下、沸点が低いため(50°C以下)、反応温度が高いと気化 することがある。その場合は、耐圧反応容器を用い、容器を密閉して前述の圧力の条 件下、前述したバッチ式にて反応を行うことができる。  [0032] In addition, 1 alkoxy 1, 1, 2, 2-tetrafluoroethane represented by the formula [1] in this reaction has a low boiling point (50 ° C or less) under normal temperature and atmospheric pressure conditions, so the reaction temperature If it is high, it may vaporize. In that case, a pressure-resistant reaction vessel is used, and the vessel can be sealed and the reaction can be carried out by the batch method described above under the conditions of the pressure described above.

[0033] ジフルォロ酢酸金属塩の精製処理の方法としては、特に限定されない。生成するジ フルォロ酢酸塩は、式 [1]で表される 1 アルコキシ 1, 1, 2, 2—テトラフルォロェ タンへの溶解度が低ぐ反応の進行とともに比較的溶解性が高いメタノール濃度が低 下すると、反応液中に KFとともに不溶性の固形混合物として析出する。固形混合物 は通常のろ過操作を組み合わせることにより容易に分離できる。固形混合物からジフ ルォロ酢酸金属塩を単離するには、 KFとの溶解度の相違を利用して、ー且メタノー ル、エタノール等の良溶媒に溶解し、エーテル、へキサン等の貧溶媒を添加して析 出、分離することができる。  [0033] The method for the purification treatment of difluoroacetic acid metal salt is not particularly limited. The resulting difluoroacetate salt has a lower solubility in 1-alkoxy 1, 1, 2, 2-tetrafluoroethane represented by the formula [1]. In the reaction solution, it precipitates with KF as an insoluble solid mixture. The solid mixture can be easily separated by combining ordinary filtration operations. To isolate difluoroacetic acid metal salt from the solid mixture, use the difference in solubility with KF and dissolve in a good solvent such as methanol or ethanol, and add a poor solvent such as ether or hexane. It can be analyzed and separated.

[0034] また、このジフルォロ酢酸塩は、塩酸、硫酸等の酸との反応によりジフルォロ酢酸と することもでき、ジフルォロ酢酸塩をー且ジフルォロ酢酸として混合物溶液力もエー テル等の溶媒により抽出、その後通常の蒸留操作にて分離することができる。 [0034] The difluoroacetate can also be converted to difluoroacetic acid by reaction with an acid such as hydrochloric acid or sulfuric acid. The difluoroacetate is then converted into difluoroacetic acid and the mixture solution power is extracted with a solvent such as ether, and then It can be separated by a normal distillation operation.

[0035] 本発明の出発原料である 1 アルコキシ 1, 1, 2, 2—テトラフルォロェタンは公 知の方法で製造できるが、例えば、耐圧反応器に所定量のメタノール及び金属水酸 化物を仕込み、テトラフルォロエチレン (TFE)を一定量導入して 1 アルコキシ 1, 1, 2, 2—テトラフルォロェタンをー且生成させた後に、本発明における方法にて反 応を進行させることによりジフルォロ酢酸金属塩を製造することもできる。  [0035] 1alkoxy 1,1,2,2-tetrafluoroethane as a starting material of the present invention can be produced by a known method. For example, a predetermined amount of methanol and a metal hydroxide are added to a pressure reactor. 1) After introducing a certain amount of tetrafluoroethylene (TFE) to form 1 alkoxy 1, 1, 2, 2-tetrafluoroethane, the reaction proceeds with the method of the present invention. It is also possible to produce a difluoroacetic acid metal salt.

[0036] 本発明により得られるジフルォロ酢酸金属塩は、医農薬の中間体および機能性材 料の中間体等に用いられるきわめて有用な化合物である。  [0036] The difluoroacetic acid metal salt obtained by the present invention is a very useful compound used as an intermediate for medical and agricultural chemicals and an intermediate for functional materials.

[0037] なお、得られたジフルォロ酢酸金属塩は、塩酸、硫酸等の酸加水分解反応により容 易にジフルォロ酢酸にすることもできる。  [0037] The obtained difluoroacetic acid metal salt can be easily converted to difluoroacetic acid by an acid hydrolysis reaction such as hydrochloric acid or sulfuric acid.

[0038] 以下に本発明を、例を挙げて具体的に説明する力 これらによって本発明は限定さ れるものではない。 実施例 1 [0038] The power to specifically describe the present invention with reference to examples below. The present invention is not limited by these. Example 1

[0039] ステンレス鋼製 lOOmllf圧反応器にメタノール 14. 60g (0. 456mol)、 1—メトキシ  [0039] Stainless steel lOOmllf pressure reactor with methanol 14.60g (0. 456mol), 1-methoxy

- 1, 1, 2, 2—テトラフルォロェタン(HFE— 254pc) 3. 01g (0. 0228mol)、水酸 化カリウム 1. l lg (0. O198mol)を仕込んだ。反応器を 50°Cに保ち 8時間反応を行 つた (変換率 100%)。反応器を氷水中で冷却後、析出した塩を減圧ろ過し、エーテ ルで洗浄した。真空乾燥後ジフルォロ酢酸カリウムとフッ化カリウムの混合物 0. 42g ( 0. 0031mol)を回収した。この回収したジフルォロ酢酸カリウムとフッ化カリウムの混 合物のモル比をイオンクロマトグラフィーにより測定したところ、ジフルォロ酢酸力リウ ム:フッ化カリウム = 1: 2であった (なお、実施例 1では単離精製は行って!/、な!/、)。 実施例 2  -1, 1, 2, 2—Tetrafluoroethane (HFE—254 pc) 3.01 g (0.0228 mol), potassium hydroxide 1. l lg (0.O198 mol) were charged. The reactor was kept at 50 ° C for 8 hours (conversion rate 100%). After cooling the reactor in ice water, the deposited salt was filtered under reduced pressure and washed with ether. After vacuum drying, 0.42 g (0.0031 mol) of a mixture of potassium difluoroacetate and potassium fluoride was recovered. When the molar ratio of the recovered mixture of potassium difluoroacetate and potassium fluoride was measured by ion chromatography, it was found to be difluoroacetate-powered potassium fluoride = 1: 2 (in Example 1, it was simply Please do the refining! /, Na! /,). Example 2

[0040] ステンレス鋼製2001111而す圧反応器にメタノール115. 2g (3. 6mol)、 1—メトキシ一 1, 1, 2, 2—テトラフルォロェタン(HFE— 254pc) 15. lg (0. 114mol)、水酸ィ匕カ リウム 11. lg (0. 198mol)を仕込んだ。反応器を 50°Cに保ち 16時間反応した (変 換率 100%)。反応器を氷水中で冷却後、析出した塩を減圧ろ過し、エーテルで洗 浄した。真空乾燥後ジフルォロ酢酸カリウムとフッ化カリウムの混合物 11. 9gを回収 した。  [0040] In a stainless steel 2001111 pressure reactor, 115.2 g (3.6 mol) of methanol, 1-methoxy-1,1,2,2-tetrafluoroethane (HFE—254 pc) 15. lg (0 114 mol) and 11. lg (0. 198 mol) of sodium hydroxide. The reactor was kept at 50 ° C for 16 hours (conversion rate 100%). After cooling the reactor in ice water, the precipitated salt was filtered under reduced pressure and washed with ether. After vacuum drying, 11.9 g of a mixture of potassium difluoroacetate and potassium fluoride was recovered.

[0041] 分液ロートに回収したジフルォロ酢酸カリウムとフッ化カリウムの混合物を全量入れ 、希塩酸を加えて酸性水溶液にした。調製した酸性水溶液力ゝらジフルォロ酢酸をジ ェチルエーテルで抽出、乾燥後、ジェチルエーテルを留去した。得られたジフルォロ 酢酸を水酸ィ匕カリウム Zメタノール溶液にて中和後ろ過し、エーテルで洗浄した。乾 燥後ジフルォロ酢酸カリウム 7. 9gが得られた。 1—メトキシ一 1, 1, 2, 2—テトラフル ォロェタンを基準としたジフルォロ酢酸カリウムの収率は 51. 7%であった。  [0041] The whole mixture of potassium difluoroacetate and potassium fluoride collected in a separatory funnel was added, and diluted hydrochloric acid was added to make an acidic aqueous solution. Difluoroacetic acid was extracted from the acidic aqueous solution prepared with dimethyl ether and dried, and then the dimethyl ether was distilled off. The obtained difluoroacetic acid was neutralized with potassium hydroxide Z methanol solution, filtered, and washed with ether. After drying, 7.9 g of potassium difluoroacetate was obtained. The yield of potassium difluoroacetate based on 1-methoxy-1,1,1,2,2-tetrafluoroethane was 51.7%.

[比較例 1]  [Comparative Example 1]

1ーメトキシ 1, 1, 2, 2—テトラフルォロェタンの代わりに 1ーメトキシェタンを用い た他は、実施例 1と温度、条件等、同様に行ったが、反応が全く進行せず、ジフルォ 口酢酸は得られな力つた (変換率 0%)。  1-Methoxy 1, 1, 2, 2-Tetrafluoroethane was used in the same manner as Example 1 except that 1-methoxyethane was used, but the reaction did not proceed at all. Acetic acid was not obtained (conversion 0%).

Claims

請求の範囲 The scope of the claims [1] 式 [1]で表される 1 アルコキシ 1, 1, 2, 2—テトラフルォロェタン  [1] 1-alkoxy 1, 1, 2, 2-tetrafluoroethane represented by the formula [1] [化 3]  [Chemical 3] H C F2 C F2 O R1 ( 1 ) HCF 2 CF 2 OR 1 (1) (ただし、 R1 は炭素数 1〜20の直鎖または分岐鎖のアルキル基を示す。)を炭素数(Wherein R 1 represents a linear or branched alkyl group having 1 to 20 carbon atoms) 1〜20のアルコールおよび、金属水酸ィ匕物もしくは金属アルコキシドと反応させること を含む、ジフルォロ酢酸金属塩の製造方法。 A method for producing a metal salt of difluoroacetate, comprising reacting with 1 to 20 alcohols and a metal hydroxide or metal alkoxide. [2] 金属水酸化物が水酸化カリウム、水酸化ナトリウム、水酸化リチウム、水酸化セシウム[2] Metal hydroxide is potassium hydroxide, sodium hydroxide, lithium hydroxide, cesium hydroxide 、水酸化マグネシウム、水酸ィ匕カルシウムよりなる群力 選ばれる少なくとも 1種である 請求項 1に記載の製造方法。 The production method according to claim 1, wherein the group force is selected from the group consisting of calcium hydroxide, calcium hydroxide and calcium hydroxide. [3] 金属アルコキシドがナトリウムメトキシド、カリウムメトキシド、ナトリウムエトキシド、力リウ ムェトキシド、ナトリウム n—プロポキシド、カリウム n—プロポキシド、ナトリウムイソプロ ポキシド、カリウムイソプロボキシドよりなる群力も選ばれる少なくとも 1種である請求項[3] At least 1 in which the metal alkoxide is selected from the group consisting of sodium methoxide, potassium methoxide, sodium ethoxide, strong rhumethoxide, sodium n-propoxide, potassium n-propoxide, sodium isopropoxide, potassium isopropoxide. Claims that are species 1に記載の製造方法。 1. The production method according to 1. [4] アルコール力メタノールであり、金属水酸化物が水酸カリウムであり、ジフルォロ酢酸 金属塩がジフルォロ酢酸カリウムである請求項 1乃至請求項 3のいずれかに記載の 製造方法。  [4] The production method according to any one of claims 1 to 3, wherein the methanol power is methanol, the metal hydroxide is potassium hydroxide, and the difluoroacetic acid metal salt is potassium difluoroacetate.
PCT/JP2006/315484 2005-08-12 2006-08-04 Process for producing difluoroacetic acid salt Ceased WO2007020816A1 (en)

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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06228043A (en) * 1993-02-05 1994-08-16 Asahi Glass Co Ltd Method for producing difluoroacetic acid
JPH0892162A (en) * 1994-07-28 1996-04-09 Asahi Glass Co Ltd Process for producing difluoroacetic acid fluoride and difluoroacetic acid ester
JP2002532442A (en) * 1998-12-11 2002-10-02 ロディア・シミ Selective hydrodehalogenation method

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06228043A (en) * 1993-02-05 1994-08-16 Asahi Glass Co Ltd Method for producing difluoroacetic acid
JPH0892162A (en) * 1994-07-28 1996-04-09 Asahi Glass Co Ltd Process for producing difluoroacetic acid fluoride and difluoroacetic acid ester
JP2002532442A (en) * 1998-12-11 2002-10-02 ロディア・シミ Selective hydrodehalogenation method

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