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JPH1149715A - Production of difluorophenols - Google Patents

Production of difluorophenols

Info

Publication number
JPH1149715A
JPH1149715A JP20655897A JP20655897A JPH1149715A JP H1149715 A JPH1149715 A JP H1149715A JP 20655897 A JP20655897 A JP 20655897A JP 20655897 A JP20655897 A JP 20655897A JP H1149715 A JPH1149715 A JP H1149715A
Authority
JP
Japan
Prior art keywords
trifluorobenzene
difluoroanisole
represented
reaction
difluorophenol
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
JP20655897A
Other languages
Japanese (ja)
Inventor
Yasushi Fukai
靖 深井
Naoto Takechi
直人 武知
Mitsuharu Shimoda
光春 下田
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.)
Kanto Denka Kogyo Co Ltd
Original Assignee
Kanto Denka Kogyo 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 Kanto Denka Kogyo Co Ltd filed Critical Kanto Denka Kogyo Co Ltd
Priority to JP20655897A priority Critical patent/JPH1149715A/en
Publication of JPH1149715A publication Critical patent/JPH1149715A/en
Pending legal-status Critical Current

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

Abstract

PROBLEM TO BE SOLVED: To efficiently produce the subject compound useful as an intermediate for medicines, agrochemicals, liquid crystals or the like by reacting a specific trifluorobenzene with sodium methoxide in an alcoholic solvent, producing a specified difluoroanisole and then hydrolyzing the resultant difluoroanisole. SOLUTION: (A) Trifluorobenzene represented by formula I (1,2,3- trifluorobenzene or the like), (B) sodium methoxide in an amount of 8-3.0 mol based on 1 mol component A and (C) an alcohol (methanol, ethanol or the like) in a volume of 2-10 ml based on 1 g component A are charged into a reactor and reacted at 60 deg.C to the boiling and refluxing temperature for 5-12 hr under stirring. A dilute hydrochloric acid is then added to neutralize the reactional mixture after the reaction. Transparent two phases are obtained and an organic phase is subsequently collected by separation. Difluoroanisole represented by formula II is then hydrolyzed in the organic phase to afford the objective compound represented by formula III (2, 5-difluorophenol or the like).

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は医薬、農薬、液晶等の重
要な中間体となりうるジフルオロフェノール類を効率よ
く製造する方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for efficiently producing difluorophenols which can be important intermediates for pharmaceuticals, agricultural chemicals, liquid crystals and the like.

【0002】[0002]

【従来の技術】従来、フルオロフェノール類の製造方法
として、1)フルオロアニリンのジアゾ化後加水分解す
る方法〔J.Am.Chem.Soc.,61.165
(1939)〕、2)アミノアニソールからシーマン反
応によりフルオロアニソールを得たのち、メトキシ基を
加水分解する方法〔日化 79,1121(197
9)〕、3)クロロフルオロベンゼンをアルカリで加水
分解する方法〔J.F1uorine Chem.,
,377,(1990)〕等が知られている。1)の
方法は実験室的には手軽にできる利点があるが、収率が
低く廃物を多量に生じるなど工業的に実用化しうる方法
とは言いがたい。2)の方法は工程が長く全体の収率が
50%以下と低い。また、シーマン反応における熱分解
反応は発熱量が大きく工業的には制御がむずかしいこ
と、副生する三フッ化ホウ素の無害化処理等厄介な問題
を含んでいる。3)の方法は反応温度が200〜300
℃と高くアルカリを使用するため反応器の腐食等工業的
には問題がある。また、我々はポリフルオロベンゼン類
をN,N−ジメチルホルムアミド等の非プロトン性極性
溶媒中ナトリウムメトキシドと反応させてフッ素が一個
減少したフルオロアニソール類を得、のち加水分解する
方法を提案した。(特願平7−294178) この方法は、収率がよく原料の入手も比較的容易なこと
から有用であるが、N,N−ジメチルホルムアミド等の
非ブロトン性極性溶媒が比較的に高価であるという欠点
を有する。
2. Description of the Related Art Conventionally, as a method for producing fluorophenols, 1) a method of diazotizing fluoroaniline followed by hydrolysis [J. Am. Chem. Soc. , 61 . 165
(1939)], 2) A method of obtaining fluoroanisole from aminoanisole by Seaman reaction and then hydrolyzing a methoxy group [Nikka 79 , 1121 (197)
9)], 3) Method of hydrolyzing chlorofluorobenzene with alkali [J. F1uorine Chem. , 5
0 , 377, (1990)]. The method 1) has an advantage that it can be easily used in a laboratory, but it cannot be said that the method is industrially practical, for example, the yield is low and a large amount of waste is generated. The method 2) has long steps and the overall yield is as low as 50% or less. In addition, the thermal decomposition reaction in the Seaman reaction involves a large amount of heat and is difficult to control industrially, and involves such troublesome problems as detoxification of boron trifluoride by-produced. In the method 3), the reaction temperature is 200 to 300.
Since an alkali is used as high as ° C., there is an industrial problem such as corrosion of a reactor. We have also proposed a method in which polyfluorobenzenes are reacted with sodium methoxide in an aprotic polar solvent such as N, N-dimethylformamide to obtain fluoroanisole having one fluorine reduced, and then hydrolyzed. (Japanese Patent Application No. 7-294178) This method is useful because the yield is high and the raw materials are relatively easy to obtain, but non-brotonic polar solvents such as N, N-dimethylformamide are relatively expensive. There is a disadvantage that there is.

【0003】[0003]

【発明が解決しようとする課題】本発明の課題は、中間
体化合物として有用なジフルオロフェノール類を効率よ
く製造できる新規な合成ルートを提供することである。
SUMMARY OF THE INVENTION An object of the present invention is to provide a novel synthetic route capable of efficiently producing difluorophenols useful as intermediate compounds.

【0004】かくして本発明者らは、鋭意検討を重ねた
結果従来法と異なる有用な製造方法を見出した。
[0004] Thus, the present inventors have conducted intensive studies and found a useful manufacturing method different from the conventional method.

【0005】[0005]

【課題を解決するための手段】本発明は、下記一般式
(I)で表されるトリフルオロベンゼン類を安価なアル
コール溶媒中ナトリウムメトキシドと反応させ、下記一
般式(II)で表されるジフルオロアニソール類とし、つ
いでこのジフルオロアニソール頬を加水分解することに
より下記一般式(III)で表されるジフルオロフェノー
ル類を得ることを特徴とするジフルオロフェノールの製
造法である:
According to the present invention, a trifluorobenzene represented by the following general formula (I) is reacted with sodium methoxide in an inexpensive alcoholic solvent to obtain a compound represented by the following general formula (II). A process for producing difluorophenols, which comprises obtaining difluoroanisole and then hydrolyzing the difluoroanisole cheek to obtain a difluorophenol represented by the following general formula (III):

【化4】 Embedded image

【化5】 Embedded image

【化6】 Embedded image

【0006】すなわち、本発明の要旨はトリフルオロベ
ンゼン類とアルコール溶媒中ナトリウムメトキシドを反
応させジフルオロアニソール類を得るという合成法を含
むジフルオロフェノール類の製造法に存する。
That is, the gist of the present invention resides in a method for producing difluorophenols including a synthesis method of reacting trifluorobenzenes with sodium methoxide in an alcohol solvent to obtain difluoroanisole.

【0007】ハロゲン化ベンゼン類とナトリウムメトキ
シドとの反応は、いわゆる芳香族求核置換反応であり、
これは通常アルコールのようなプロトン性の溶媒中では
進行しにくい。事実モノフルオロベンゼン及びジフルオ
ロベンゼン類はアルコール溶媒中で当該反応がほとんど
進行しない。我々は鋭意検討した結果、意外にもトリフ
ルオロベンゼン類とナトリウムメトキシドがアルコール
溶媒中で比較的穏和な条件下で顕著に反応し、ジフルオ
ロアニソール類が生成することを見いだし本発明に到達
した。本発明ではその反応生成物をさらに公知法で加水
分解することにより、ジフルオロフェノール類を得る。
The reaction between halogenated benzenes and sodium methoxide is a so-called aromatic nucleophilic substitution reaction,
This usually does not easily proceed in protic solvents such as alcohols. In fact, the reaction of monofluorobenzene and difluorobenzene hardly proceeds in an alcohol solvent. As a result of our intensive studies, we have surprisingly found that trifluorobenzenes and sodium methoxide react significantly in an alcohol solvent under relatively mild conditions to produce difluoroanisole, and arrived at the present invention. In the present invention, difluorophenols are obtained by further hydrolyzing the reaction product by a known method.

【0008】本発明の具体的な実施に際しては、反応器
に一般式(1)で表されるトリフルオロベンゼン類、ア
ルコールおよびナトリウムメトキシドを仕込み、撹拌下
に所定温度で所定時間反応させる。この反応が本発明の
中心となるものである。反応後、希塩酸を加えて中和
し、透明2液相としたのち有機相を分取する。有機相中
のジフルオロアニソールは通常の方法、例えば蒸留など
により容易に分離精製できる。得られたフルオロアニソ
ール類を常法により加水分解し、目的とする一般式(II
I)で表されるジフルオロフェノールに変換する。
In the concrete implementation of the present invention, trifluorobenzenes represented by the general formula (1), alcohol and sodium methoxide are charged into a reactor and reacted at a predetermined temperature and a predetermined time under stirring. This reaction is central to the present invention. After the reaction, the mixture is neutralized by adding dilute hydrochloric acid to obtain two transparent liquid phases, and then the organic phase is separated. Difluoroanisole in the organic phase can be easily separated and purified by a usual method, for example, distillation. The obtained fluoroanisole is hydrolyzed by a conventional method to obtain the desired compound represented by the general formula (II)
Converted to difluorophenol represented by I).

【0009】本発明の主反応(I→II)に用いるアルコ
ール溶媒としては、メタノール、エタノール、1−プロ
パノール、2−プロパノール等を挙げることができる。
Examples of the alcohol solvent used in the main reaction (I → II) of the present invention include methanol, ethanol, 1-propanol and 2-propanol.

【0010】溶媒の好ましい使用量は原料のトリフルオ
ロベンゼン類1gに対して2〜10mlの割合である。
The preferred amount of the solvent used is 2 to 10 ml per 1 g of the starting trifluorobenzenes.

【0011】ナトリウムメトキシドの好ましい使用量は
トリフルオロベンゼン類の単位モル当たり0.8〜3.
0モルである。
The preferred amount of sodium methoxide used is 0.8 to 3 per unit mole of trifluorobenzenes.
0 mol.

【0012】本発明の主反応の反応温度は、60℃〜沸
騰還流温度が好まい。また、反応時間は5〜12時間で
ある。
The reaction temperature of the main reaction of the present invention is preferably from 60 ° C. to the boiling reflux temperature. The reaction time is 5 to 12 hours.

【0013】本発明の一般式(I)に示すトリフルオロ
ベンゼン類は1,2,3−トリフルオロベンゼン、1,
2,4−トリフルオロベンゼン、1,3,5−トリフル
オロベンゼンのいずれかである。一般式(III)の本発
明方法の目的生成物のジフルオロフェノール類は、2,
5−ジフルオロフェノール、3,5−ジフルオロフェノ
ール、2,3−ジフルオロフェノールおよび2,6−ジ
フルオロフェノールのいずれかである。
The trifluorobenzenes represented by the general formula (I) of the present invention are 1,2,3-trifluorobenzene,
Any of 2,4-trifluorobenzene and 1,3,5-trifluorobenzene. The difluorophenols which are the desired products of the process of the invention of the general formula (III) are 2,2
Any of 5-difluorophenol, 3,5-difluorophenol, 2,3-difluorophenol and 2,6-difluorophenol.

【0014】加水分解工程は適宜の公知方法で実施で
き、例えば以下の実施例に記載した方式で都合よくおこ
なうことができる。
The hydrolysis step can be carried out by any suitable known method, for example, conveniently by the method described in the following Examples.

【0015】[0015]

【実施例】2,5−ジフルオロフェノールの製造 実施例1 100mlガラス製三つ口フラスコに1,2,4−トリ
フルオロベンゼン13.2g(0.100mol)、ナ
トリウムメトキシド10.8g(0.200mol)、
メタノール35mlを仕込む。マグネチックスターラー
撹拌下、浴温90℃で9時間反応させた。反応終了後、
希塩酸を加えて中和し、つぎにこれを分液ロートに移し
有機相を分取した。NMR分析により、反応物の組成は
2,5−ジフルオロアニソール89.5%、2,4−ジ
フルオロアニソール0.9%および1,2,4−トリフ
ルオロベンゼン9.6%であった。これを蒸留し2,5
−ジフルオロアニソール11.5gを得た。つぎに、こ
の2,5−ジフルオロアニソール11.5gと47%臭
化水素酸溶液100gを200mlガラス製三つ口フラ
スコに入れ、18時間加熱還流し加水分解反応をおこな
った。放冷後ジクロロメタン100mlで抽出し、つぎ
にジクロロメタンを留去させる。この濃縮残さを蒸留
し、2,5−ジフルオロフェノールを得た。収量7.3
g、収率56%(トリフルオロベンゼン基準)であっ
た。
EXAMPLES Production of 2,5-difluorophenol Example 1 In a 100 ml glass three-necked flask, 13.2 g (0.100 mol) of 1,2,4-trifluorobenzene and 10.8 g of sodium methoxide (0.10 mol) were added. 200 mol),
35 ml of methanol are charged. The reaction was carried out at a bath temperature of 90 ° C. for 9 hours under magnetic stirring. After the reaction,
The mixture was neutralized by adding dilute hydrochloric acid, and then transferred to a separating funnel to separate the organic phase. According to NMR analysis, the composition of the reaction product was 89.5% of 2,5-difluoroanisole, 0.9% of 2,4-difluoroanisole and 9.6% of 1,2,4-trifluorobenzene. Distill this, 2,5
-11.5 g of difluoroanisole were obtained. Next, 11.5 g of this 2,5-difluoroanisole and 100 g of a 47% hydrobromic acid solution were put into a 200 ml glass three-necked flask, and heated under reflux for 18 hours to carry out a hydrolysis reaction. After allowing to cool, the mixture is extracted with 100 ml of dichloromethane, and then dichloromethane is distilled off. The concentrated residue was distilled to obtain 2,5-difluorophenol. Yield 7.3
g, the yield was 56% (based on trifluorobenzene).

【0016】実施例2 溶媒のメタノールをエタノールに代えた以外は実施例1
と同様の手順でおこなった。
Example 2 Example 1 except that methanol was used as the solvent instead of ethanol.
The same procedure was used.

【0017】2,5−ジフルオロフェノールの収量7.
1g、収率55%(トリフルオロベンゼン基準)であっ
た。
6. Yield of 2,5-difluorophenol
The yield was 1 g and 55% (based on trifluorobenzene).

【0018】3,5−ジフルオロフェノールの製造 実施例3 原料の1,2,4−トリフルオロベンゼンを1,3,5
−トリフルオロベンゼンに代えた以外は実施例1と同様
の手順でおこなった。
Production of 3,5-difluorophenol Example 3 1,2,4-trifluorobenzene as a raw material was converted to 1,3,5
-The procedure was the same as in Example 1, except that trifluorobenzene was used.

【0019】3,5−トリルオロフェノールの収量6.
1g、収率47%(トリフルオロベンゼン基準)であっ
た。
5. Yield of 3,5-tolylphenol
The yield was 1 g and 47% (based on trifluorobenzene).

【0020】2,3−ジフルオロフェノールおよび2,
6−ジフルオロフェノールの製造 実施例4 原料の1,2,4−トリフルオロベンゼンを1,2,3
−トリフルオロベンゼンに代え、他は実施例1と同様の
手順でおこなった。但し、アニソールを単離する方法と
して精留により2,3−ジフルオロアニソールと2,6
−ジフルオロアニソールに分けた。そして各々のアニソ
ールについて加水分解反応を実施した。
2,3-difluorophenol and 2,
Production of 6-difluorophenol Example 4 Starting material 1,2,4-trifluorobenzene was replaced with 1,2,3
-The procedure was the same as that of Example 1, except that trifluorobenzene was used. However, as a method for isolating anisole, 2,3-difluoroanisole and 2,6
-Divided into difluoroanisole. And hydrolysis reaction was implemented about each anisole.

【0021】2,3−ジフルオロフェノールの収量5.
0g、2,6−ジフルオロフェノールの収量2.8gで
トータル収量7.8g、収率60%(トリフルオロベン
ゼン基準)であった。
4. Yield of 2,3-difluorophenol
0 g and 2.8 g of 2,6-difluorophenol were obtained, and the total yield was 7.8 g and the yield was 60% (based on trifluorobenzene).

【0022】実施例5 溶媒のメタノールを2−プロパノールに代えた以外は実
施例4と同様の手順でおこなった。
Example 5 The same procedure as in Example 4 was carried out except that the solvent, methanol, was replaced with 2-propanol.

【0023】2,3−ジフルオロフェノールの収量5.
0g、2,6−ジフルオロフェノールの収量2.5gで
トータル収量7.5g、収率58%(トリフルオロベン
ゼン基準)であった。
4. Yield of 2,3-difluorophenol
The total yield was 7.5 g with a yield of 0 g and 2,6-difluorophenol of 2.5 g, and a yield of 58% (based on trifluorobenzene).

【0024】実施例6 溶媒のメタノールを1−プロパノールに代えた以外は実
施例4と同様の手順でおこなった。
Example 6 The same procedure as in Example 4 was carried out except that the solvent, methanol, was replaced with 1-propanol.

【0025】2,3−ジフルオロフェノールの収量5.
2g、2,6−ジフルオロフェノールの収量2.6gで
トータル収量7.8g 、収率60%(トリフルオロベ
ンゼン基準)であった。
4. Yield of 2,3-difluorophenol
The total yield was 2 g, 2.6 g of 2,6-difluorophenol was 7.8 g, and the yield was 60% (based on trifluorobenzene).

【発明の効果】本発明の方法によれば、既存の方法より
も穏和な条件下、かつ安価な溶媒の使用によりフルオロ
フェノール類を有利に製造することができる。
According to the method of the present invention, fluorophenols can be advantageously produced under milder conditions than the existing methods and by using an inexpensive solvent.

─────────────────────────────────────────────────────
────────────────────────────────────────────────── ───

【手続補正書】[Procedure amendment]

【提出日】平成9年8月29日[Submission date] August 29, 1997

【手続補正1】[Procedure amendment 1]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0002[Correction target item name] 0002

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0002】[0002]

【従来の技術】従来、フルオロフェノール類の製造方法
として、1)フルオロアニリンのジアゾ化後加水分解す
る方法〔J.Am.Chem.Soc.,61.165
(1939)〕、2)アミノアニソールからシーマン反
応によりフルオロアニソールを得たのち、メトキシ基を
加水分解する方法〔日化 79,1121(197
9)〕、3)クロロフルオロベンゼンをアルカリで加水
分解する方法〔J.F1uorine Chem.,
,377,(1990)〕等が知られている。1)の
方法は実験室的には手軽にできる利点があるが、収率が
低く廃物を多量に生じるなど工業的に実用化しうる方法
とは言いがたい。2)の方法は工程が長く全体の収率が
50%以下と低い。また、シーマン反応における熱分解
反応は発熱量が大きく工業的には制御がむずかしいこ
と、副生する三フッ化ホウ素の無害化処理等厄介な問題
を含んでいる。3)の方法は反応温度が200〜300
℃と高くアルカリを使用するため反応器の腐食等工業的
には問題がある。また、我々はポリフルオロベンゼン類
をN,N−ジメチルホルムアミド等の非プロトン性極性
溶媒中ナトリウムメトキシドと反応させてフッ素が一個
減少したフルオロアニソール類を得、のち加水分解する
方法を提案した。(特願平7−294178) この方法は、収率がよく原料の入手も比較的容易なこと
から有用であるが、N,N−ジメチルホルムアミド等の
非プロトン性極性溶媒が比較的に高価であるという欠点
を有する。
2. Description of the Related Art Conventionally, as a method for producing fluorophenols, 1) a method of diazotizing fluoroaniline followed by hydrolysis [J. Am. Chem. Soc. , 61 . 165
(1939)], 2) A method of obtaining fluoroanisole from aminoanisole by Seaman reaction and then hydrolyzing a methoxy group [Nikka 79 , 1121 (197)
9)], 3) Method of hydrolyzing chlorofluorobenzene with alkali [J. F1uorine Chem. , 5
0 , 377, (1990)]. The method 1) has an advantage that it can be easily used in a laboratory, but it cannot be said that the method is industrially practical, for example, the yield is low and a large amount of waste is generated. The method 2) has long steps and the overall yield is as low as 50% or less. In addition, the thermal decomposition reaction in the Seaman reaction involves a large amount of heat and is difficult to control industrially, and involves such troublesome problems as detoxification of boron trifluoride by-produced. In the method 3), the reaction temperature is 200 to 300.
Since an alkali is used as high as ° C., there is an industrial problem such as corrosion of a reactor. We have also proposed a method in which polyfluorobenzenes are reacted with sodium methoxide in an aprotic polar solvent such as N, N-dimethylformamide to obtain fluoroanisole having one fluorine reduced, and then hydrolyzed. (Japanese Patent Application No. 7-294178) This method is useful because the yield is high and the raw materials are relatively easy to obtain, but an aprotic polar solvent such as N, N-dimethylformamide is relatively expensive. There is a disadvantage that there is.

【手続補正2】[Procedure amendment 2]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0008[Correction target item name] 0008

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0008】本発明の具体的な実施に際しては、反応器
に一般式(1)で表されるトリフルオロベンゼン類、ア
ルコールおよびナトリウムメトキシドを仕込み、撹拌下
に所定温度で所定時間反応させる。この反応が本発明の
中心となるものである。反応後、希塩酸を加えて中和
し、透明2液相としたのち有機相を分取する。有機相中
のジフルオロアニソールは通常の方法、例えば蒸留など
により容易に分離精製できる。得られたジフルオロアニ
ソール類を常法により加水分解し、目的とする一般式
(III)で表されるジフルオロフェノールに変換する。
In the concrete implementation of the present invention, trifluorobenzenes represented by the general formula (1), alcohol and sodium methoxide are charged into a reactor and reacted at a predetermined temperature and a predetermined time under stirring. This reaction is central to the present invention. After the reaction, the mixture is neutralized by adding dilute hydrochloric acid to obtain two transparent liquid phases, and then the organic phase is separated. Difluoroanisole in the organic phase can be easily separated and purified by a usual method, for example, distillation. The obtained difluoroanisole is hydrolyzed by a conventional method, and is converted into a desired difluorophenol represented by the general formula (III).

【手続補正3】[Procedure amendment 3]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0012[Correction target item name] 0012

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0012】本発明の主反応の反応温度は、60℃〜沸
騰還流温度が好ましい。また、反応時間は5〜12時間
である。
[0012] The reaction temperature of the main reaction of the present invention is preferably from 60 ° C to the boiling reflux temperature. The reaction time is 5 to 12 hours.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 下記一般式(1)で表されるトリフルオ
ロベンゼン類とナトリウムメトキシドをアルコール溶媒
中で反応させることにより下記一般式(II)で表される
ジフルオロアニソール類を得、つぎに加水分解反応によ
り下記一般式(III)で表されるジフルオロフェノール
を得ることを特徴とするジフルオロフェノール類の製造
法。 【化1】 【化2】 【化3】
1. A difluoroanisole represented by the following general formula (II) is obtained by reacting a trifluorobenzene represented by the following general formula (1) with sodium methoxide in an alcohol solvent. A process for producing difluorophenols, comprising obtaining a difluorophenol represented by the following general formula (III) by a hydrolysis reaction. Embedded image Embedded image Embedded image
JP20655897A 1997-07-31 1997-07-31 Production of difluorophenols Pending JPH1149715A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20655897A JPH1149715A (en) 1997-07-31 1997-07-31 Production of difluorophenols

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20655897A JPH1149715A (en) 1997-07-31 1997-07-31 Production of difluorophenols

Publications (1)

Publication Number Publication Date
JPH1149715A true JPH1149715A (en) 1999-02-23

Family

ID=16525391

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20655897A Pending JPH1149715A (en) 1997-07-31 1997-07-31 Production of difluorophenols

Country Status (1)

Country Link
JP (1) JPH1149715A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105593196A (en) * 2013-10-04 2016-05-18 巴斯夫欧洲公司 Selective hydrolysis and alcoholysis of chlorinated benzenes
CN107793295A (en) * 2016-08-30 2018-03-13 上海伟和生物科技有限公司 A kind of preparation method of 3,5 difluorophenol

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105593196A (en) * 2013-10-04 2016-05-18 巴斯夫欧洲公司 Selective hydrolysis and alcoholysis of chlorinated benzenes
US20160289157A1 (en) * 2013-10-04 2016-10-06 Basf Se Selective hydrolysis and alcoholysis of chlorinated benzenes
US10093607B2 (en) * 2013-10-04 2018-10-09 Basf Se Selective hydrolysis and alcoholysis of chlorinated benzenes
CN107793295A (en) * 2016-08-30 2018-03-13 上海伟和生物科技有限公司 A kind of preparation method of 3,5 difluorophenol

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