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JPS60258143A - Production of 2,3,5,6-tetrafluorobenzoic acid - Google Patents

Production of 2,3,5,6-tetrafluorobenzoic acid

Info

Publication number
JPS60258143A
JPS60258143A JP11388384A JP11388384A JPS60258143A JP S60258143 A JPS60258143 A JP S60258143A JP 11388384 A JP11388384 A JP 11388384A JP 11388384 A JP11388384 A JP 11388384A JP S60258143 A JPS60258143 A JP S60258143A
Authority
JP
Japan
Prior art keywords
acid
zinc
aqueous solution
tetrafluorobenzoic
pentafluorobenzoic acid
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.)
Pending
Application number
JP11388384A
Other languages
Japanese (ja)
Inventor
Nobuo Tominaga
信雄 富永
Osamu Kaieda
修 海江田
Tomoaki Nakamura
智明 中村
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.)
Nippon Shokubai Co Ltd
Original Assignee
Nippon Shokubai Co 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 Nippon Shokubai Co Ltd filed Critical Nippon Shokubai Co Ltd
Priority to JP11388384A priority Critical patent/JPS60258143A/en
Publication of JPS60258143A publication Critical patent/JPS60258143A/en
Pending legal-status Critical Current

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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

PURPOSE:To prepare the titled compound useful as a raw material for photosensitive agent, etc. in high yield without passing through an intermediate, by reacting as pentafluorobenzoic acid with zinc in an alkaline aqueous solution within a specific temperature range. CONSTITUTION:Pentafluorobenzoic acid is reacted with zinc in an alkaline aqueous solution containing lithium hydroxide, sodium hydroxide, potassium carbonate or ethylenediamine, within about 20-100 deg.C, preferably 40-70 deg.C temperature range to give the aimed 2,3,5,6-tetrafluorobenzoic acid. The amount of the alkali to be used is preferably 3-5mol based on 1mol pentafluorobenzoic acid, and the amount of the zinc to be used is preferably 1.0-2.5mol based on 1mol pentafluorobenzoic acid.

Description

【発明の詳細な説明】 本発明は、ペンタフルオロ安息香酸をアルカリ性水溶液
中約20〜100℃の温度で亜鉛と反応させて2.3.
5.6−テトラフルオロ安息香酸を製造する方法に関す
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention comprises reacting pentafluorobenzoic acid with zinc in an alkaline aqueous solution at a temperature of about 20-100°C to produce 2.3.
The present invention relates to a method for producing 5.6-tetrafluorobenzoic acid.

2、3.5.6−テトラフルオロ安息香酸は、感光剤な
どの原料として有用なものである。
2,3.5.6-tetrafluorobenzoic acid is useful as a raw material for photosensitizers and the like.

2、3.5.6−テトラフルオロ安息香酸を合成する方
法は、J、Chem 8oc、、 1965年、634
1頁に記載されている。
A method for synthesizing 2,3.5.6-tetrafluorobenzoic acid is described in J. Chem 8oc., 1965, 634.
It is written on page 1.

上記の方法は、まずペンタフルオロ安息香酸とヒドラジ
ンと反応させて、2,3,5.6−テトラフルオロ−4
−ヒドラジノ安息香酸を合成し、ついでその2.3.5
.6−テトラフルオロ−4−ヒドラジノ安息香酸を硫酸
銅水溶液で反応させて2、3.5.6−テトラフルオロ
安息香酸をえている。
The above method involves first reacting pentafluorobenzoic acid with hydrazine to obtain 2,3,5,6-tetrafluoro-4
-Synthesize hydrazinobenzoic acid and then 2.3.5
.. 2,3.5.6-tetrafluorobenzoic acid is obtained by reacting 6-tetrafluoro-4-hydrazinobenzoic acid with an aqueous copper sulfate solution.

しかしながら、この方法においては、きわめて収率が低
く、また工程が長いという欠点を有しており、工業的実
施の面では不充分な製造法である。
However, this method has the drawbacks of extremely low yield and long steps, making it an insufficient production method for industrial implementation.

本発明者らは、上記の欠点を改良するために鋭意検討し
た結果、ペンタフルオロ安息香酸なアルカリ性水溶液中
約20〜100℃の温度範囲で亜鉛と反応させることに
よって2.3,5.6−テトラフルオロ安息香酸を高収
率で、しかもペンタフルオロ安息香酸から中間体を経ず
一段で製造できることを見い出し本発明を完成させた。
As a result of intensive studies to improve the above-mentioned drawbacks, the present inventors discovered that 2.3,5.6-2.3,5.6- The present inventors have discovered that tetrafluorobenzoic acid can be produced in high yield from pentafluorobenzoic acid in one step without passing through any intermediates, and have completed the present invention.

本発明においてアルカリ水溶液を調製するために使用す
るアルカリ性物質としては、水酸化リチウム、水酸化ナ
トリウム、水酸化カリウムあるいは水酸化セシウムのよ
うなアルカリ金属水酸化物、炭酸カリウムあるいは酸化
カルシウムなどのように水溶液中でアルカリ性物質に解
離あるいは変化するものならばあらゆるものが使用でき
る。またエチレンジアミン、トリエチルアミンなどの有
機アミン類およびアンモニア等のアルカリ性を示すもの
ならばあらゆるものが使用できる。
In the present invention, the alkaline substances used to prepare the alkaline aqueous solution include alkali metal hydroxides such as lithium hydroxide, sodium hydroxide, potassium hydroxide, or cesium hydroxide, potassium carbonate, and calcium oxide. Any substance that dissociates or changes into an alkaline substance in an aqueous solution can be used. Furthermore, any organic amines such as ethylenediamine and triethylamine, and anything showing alkalinity such as ammonia can be used.

本発明者らは、アルカリ性物質としてKOHを用いる場
合本発明の方法は下記(1)の反応式に従って反応して
いると推定している。
The present inventors estimate that when KOH is used as the alkaline substance, the method of the present invention reacts according to the reaction formula (1) below.

従って使用するアルカリ量は、理論的にはペンタフルオ
ロ安息香酸1モルに対して2モル倍以上存在すれば良い
が、好ましくは3〜5モル倍存在させるのが良い。また
アルカリ濃度は仕込むペンタフルオロ安息香酸の濃度に
よっても変わるが、一般的には5〜20重量%になるよ
うに調整するのが望ましい。
Therefore, the amount of alkali used should theoretically be 2 times or more by mole per 1 mole of pentafluorobenzoic acid, but preferably 3 to 5 times by mole. Although the alkali concentration varies depending on the concentration of pentafluorobenzoic acid to be charged, it is generally desirable to adjust it to 5 to 20% by weight.

亜鉛は、通常市販されている金属亜鉛末などあらゆるも
のを使用することができる。使用する亜鉛量は、上記反
応式(1)に従って理論的にはぺ/タフルオロ安息香酸
1モルに対して、1モル以上存在すれば良いが、通常1
.05〜2.5モル倍存在させるのが好ましい。
Any zinc can be used, such as commercially available metal zinc powder. The amount of zinc to be used should theoretically be 1 mol or more per 1 mol of pe/tafluorobenzoic acid according to the above reaction formula (1), but it is usually 1 mol or more.
.. It is preferable to make it exist in an amount of 0.5 to 2.5 moles.

本発明では、反応温度20〜100°Cの範囲で反応さ
せることができるが、反応温度が低い程、反応速度が低
下するので反応時間を長くする必要があり生産性が低下
する。また反応温度が高い場合テトラフルオロ−4−ヒ
ドロキシ−安息香酸が多量に副生ずるので好ましくない
In the present invention, the reaction can be carried out at a reaction temperature in the range of 20 to 100°C, but the lower the reaction temperature is, the lower the reaction rate is, so the reaction time needs to be longer, resulting in lower productivity. Further, if the reaction temperature is high, a large amount of tetrafluoro-4-hydroxybenzoic acid is produced as a by-product, which is not preferable.

従って40〜70℃の温度範囲で行なうのが特に好まし
い。また段階的に低い温度から高温度に昇温させながら
反応させても良い。 “°□:反応時間は、通常5時間
〜48時間の範囲で行なうのが良い。
Therefore, it is particularly preferable to conduct the reaction at a temperature in the range of 40 to 70°C. Alternatively, the reaction may be carried out while raising the temperature stepwise from a low temperature to a high temperature. "°□: The reaction time is usually preferably carried out in a range of 5 hours to 48 hours.

反応終了後の生成物は、r過等の手段によって固形物を
分離後、その水溶液にPH1〜6になるように硫酸ある
いは塩酸等の酸性水溶液を加えて、いわゆる酸析を行な
い2.3.5.6−テトラフルオロ安息香酸を生成させ
る。
After the reaction is completed, solid matter is separated from the product by means such as r-filtration, and then an acidic aqueous solution such as sulfuric acid or hydrochloric acid is added to the aqueous solution to adjust the pH to 1 to 6 to perform so-called acid precipitation 2.3. 5. Generate 6-tetrafluorobenzoic acid.

酸析後えられた2、 3.5.6−テトラフルオロ安息
香酸を含有する水溶液から2.3.5.6−テトラフル
オロ安息香酸を分離するには、抽出溶媒、例えばエーテ
ル、塩化メチレン、ベンゼン、トルエン等を使って、2
,3,5.6−テトラフルオロ安息香酸を有機層に抽出
し分液後蒸発乾固することによって可能である。必要な
らばこの製品を更に再結晶等の方法によって精製するこ
ともできる。
To separate 2.3.5.6-tetrafluorobenzoic acid from the aqueous solution containing 2,3.5.6-tetrafluorobenzoic acid obtained after acid precipitation, an extraction solvent such as ether, methylene chloride, 2 using benzene, toluene, etc.
, 3,5.6-tetrafluorobenzoic acid is extracted into an organic layer, separated and then evaporated to dryness. If necessary, this product can be further purified by methods such as recrystallization.

以下本発明を実施例によりさらに具体的に説明するが、
本発明はこれらに限定されるものではない。
Hereinafter, the present invention will be explained in more detail with reference to Examples.
The present invention is not limited to these.

実施例1 500WLl三つロフラスコに水酸化カリウム21.2
2(0,377モル)を溶解させた水溶液280m1を
仕込み、ついでペンタフルオロ安息香酸20.0f(0
,0943モル)と亜鉛末12.49(0,19モル)
を加え、60℃で24時間撹拌させながら加熱させた。
Example 1 Potassium hydroxide 21.2 in a 500 WLl three-necked flask
2 (0,377 mol) was charged, and then 20.0 f (0,377 mol) of pentafluorobenzoic acid was charged.
,0943 mol) and zinc powder 12.49 (0.19 mol)
was added and heated at 60°C for 24 hours with stirring.

次に放冷後沢過し固形物を分離させ、次いでこの母液に
PI(が1.7になるように6規定硫酸水溶液を滴下し
て中和し、2.3.5.6−テトラフルオロ安息香酸を
えた。えられた2、3,5,6−テトラフルオロ安息香
酸を含む水溶液にエーテル200ccを加え、有機層に
2.3.5.6−テトラフルオロ安息香酸を抽出した。
Next, after cooling, the solid matter was separated by filtering, and then a 6N aqueous sulfuric acid solution was added dropwise to this mother liquor so that PI (PI) was 1.7 to neutralize it. Benzoic acid was obtained. 200 cc of ether was added to the obtained aqueous solution containing 2,3,5,6-tetrafluorobenzoic acid, and 2.3.5.6-tetrafluorobenzoic acid was extracted from the organic layer.

この抽出操作を3回繰返し、見られたエーテル層を水s
odで洗浄後蒸発乾固した。この蒸発乾固した製品を液
体クロマトグラフィー(カラム充填剤; ODS系、キ
ャリア溶媒;メタノール・燐酸二水素ナトリウム混合水
溶液)を用いて、2,5−ジl弘安息香酸を内部標準物
質として用い分析したところ、仕込みのペンタフルオロ
安息香酸に対して、2.3.5.6−テトラフルオロ安
息香酸81.6モルチ、テトラフルオロ−4−ヒト四キ
シ安息香酸9.6モル%の収率で目的物質かえられてい
た。
This extraction operation was repeated three times, and the ether layer was extracted with water.
After washing with OD and evaporating to dryness. The evaporated product was analyzed using liquid chromatography (column packing: ODS system, carrier solvent: methanol/sodium dihydrogen phosphate mixed aqueous solution) using 2,5-dil-benzoic acid as an internal standard. As a result, the desired yield was 81.6 mol% of 2.3.5.6-tetrafluorobenzoic acid and 9.6 mol% of tetrafluoro-4-human tetraxybenzoic acid based on the charged pentafluorobenzoic acid. Substances had changed.

この製品を水を用いて再結晶を行って、151〜152
℃の融点を有する2、 3.5.6−テトラフルオロ安
息香酸の純品をえた。この純品を用いて元素分析を行な
いえられた物質が2t L 5+ 6−テトラフルオロ
安息香酸であることを確認した。
This product was recrystallized using water to give 151 to 152
Pure 2,3.5.6-tetrafluorobenzoic acid with a melting point of .degree. C. was obtained. Elemental analysis using this pure product confirmed that the substance was 2t L 5+ 6-tetrafluorobenzoic acid.

元素分析値 C(%) H(憾) F(り理論値 43
.34 1.03 39.18分析値 42.9 1.
1 38.9
Elemental analysis value C (%) H (regret) F (ri) Theoretical value 43
.. 34 1.03 39.18 Analysis value 42.9 1.
1 38.9

Claims (1)

【特許請求の範囲】 (11ペンタフルオロ安息香酸をアルカリ性水溶液中約
20〜100’Cの温度範囲で亜鉛と反応させることを
特徴とする2、 3.5.6−テトラフルオロ安息香酸
の製造方法。 (2)反応が40〜70℃の温度範囲で行なわれること
を特徴とする特許請求の範囲(1)記載の方法。
[Claims] (A process for producing 2,3,5,6-tetrafluorobenzoic acid, which comprises reacting 11-pentafluorobenzoic acid with zinc in an alkaline aqueous solution at a temperature range of about 20 to 100'C. (2) The method according to claim (1), wherein the reaction is carried out at a temperature range of 40 to 70°C.
JP11388384A 1984-06-05 1984-06-05 Production of 2,3,5,6-tetrafluorobenzoic acid Pending JPS60258143A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11388384A JPS60258143A (en) 1984-06-05 1984-06-05 Production of 2,3,5,6-tetrafluorobenzoic acid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11388384A JPS60258143A (en) 1984-06-05 1984-06-05 Production of 2,3,5,6-tetrafluorobenzoic acid

Publications (1)

Publication Number Publication Date
JPS60258143A true JPS60258143A (en) 1985-12-20

Family

ID=14623509

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11388384A Pending JPS60258143A (en) 1984-06-05 1984-06-05 Production of 2,3,5,6-tetrafluorobenzoic acid

Country Status (1)

Country Link
JP (1) JPS60258143A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6456656A (en) * 1987-05-27 1989-03-03 Nippon Carbide Kogyo Kk Production of 2,3,5,6-tetrafluorobenzonitrile
US4822912A (en) * 1987-02-20 1989-04-18 Bayer Aktiengesellschaft Process for the preparation of 2,3,5,6-tetrafluorobenzoic acid
EP0514863A2 (en) * 1991-05-22 1992-11-25 Hoechst Aktiengesellschaft Process for preparing 3,4,6-trifluorophthalic acid and its anhydride
EP0563986A2 (en) * 1992-04-03 1993-10-06 Occidental Chemical Corporation Process for selective hydrodefluorination
CN107759468A (en) * 2017-11-22 2018-03-06 大连奇凯医药科技有限公司 The preparation method of 2,3,5,6 tetrafluorobenzoic aids

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4822912A (en) * 1987-02-20 1989-04-18 Bayer Aktiengesellschaft Process for the preparation of 2,3,5,6-tetrafluorobenzoic acid
JPS6456656A (en) * 1987-05-27 1989-03-03 Nippon Carbide Kogyo Kk Production of 2,3,5,6-tetrafluorobenzonitrile
EP0514863A2 (en) * 1991-05-22 1992-11-25 Hoechst Aktiengesellschaft Process for preparing 3,4,6-trifluorophthalic acid and its anhydride
EP0563986A2 (en) * 1992-04-03 1993-10-06 Occidental Chemical Corporation Process for selective hydrodefluorination
EP0563986A3 (en) * 1992-04-03 1994-11-23 Occidental Chem Co Process for selective hydrodefluorination
CN1038745C (en) * 1992-04-03 1998-06-17 西方化学公司 Process for selective hydrodefluorination
CN107759468A (en) * 2017-11-22 2018-03-06 大连奇凯医药科技有限公司 The preparation method of 2,3,5,6 tetrafluorobenzoic aids

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