JPH05988A - Production of trifluoroanisole compounds - Google Patents

Production of trifluoroanisole compounds

Info

Publication number
JPH05988A
JPH05988A JP3181851A JP18185191A JPH05988A JP H05988 A JPH05988 A JP H05988A JP 3181851 A JP3181851 A JP 3181851A JP 18185191 A JP18185191 A JP 18185191A JP H05988 A JPH05988 A JP H05988A
Authority
JP
Japan
Prior art keywords
same
group
compound
atom
trifluoroanisole
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
JP3181851A
Other languages
Japanese (ja)
Inventor
Seisaku Kumai
清作 熊井
Seiji Shintani
清治 新谷
Takashi Seki
隆司 関
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.)
AGC Inc
Original Assignee
Asahi Glass 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 Asahi Glass Co Ltd filed Critical Asahi Glass Co Ltd
Priority to JP3181851A priority Critical patent/JPH05988A/en
Publication of JPH05988A publication Critical patent/JPH05988A/en
Pending legal-status Critical Current

Links

Classifications

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

Abstract

PURPOSE:To simply and inexpensively produce the subject compound useful as an intermediate for medicines, agricultural chemicals, etc., by reacting a halogenated anisole compound with hydrofluoric acid in the presence of a specific fluorination catalyst. CONSTITUTION:A compound of formula I (X is C1, BR; R<1> is halogen, alkyl, alkoxy, etc.; (n) is 1, 2; (m) is 0-5; but (m+n)<=6; (p) is 0-3; (q) is 0-2; but (p+q)=3) is allowed to react with hydrofluoric acid, preferably hydrofluoric anhydride (preferably in an amount of 3.3-10 time moles per mole of the compound of formula I) in the presence of the halide compound of a metal selected from iron, aluminum, molybdenum, titanium and antimony (preferably in an amount of 0.1-10mol.% based on the compound of formula I) preferably at -10 to 50 deg.C to produce the objective compound of formula II (R<2> is the same as R<1>, but R<2> placed at the same position as R<1> is the same atom or group; and When plural R<1> exist, R<1> groups are also the same; but when fluorine is excluded from the a halogen, R<2> is F, etc.,), such as 0-chloro-alpha,alpha,alphatrifluoroanisole.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は医薬中間体、農薬中間
体、液晶等の機能性材料中間体として有用なトリフルオ
ロアニソール類の製造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 producing trifluoroanisole which is useful as an intermediate for functional materials such as pharmaceutical intermediates, agricultural chemical intermediates and liquid crystals.

【0002】[0002]

【従来の技術】トリフルオロアニソール類の製造方法と
して従来、次の方法が知られている。 (1)トリクロロアニソール類を三フッ化アンチモンで
フッ素化する方法(EP 140,783)あるいはフッ化水素
酸でフッ素化する方法(USP 4,876,376)。 (2)フェノール類をフッ化水素酸中、四塩化炭素と反
応させることにより、トリクロロメチル化、フッ素化を
同時に行う方法(USP 4,157,344)。 (3)トリクロロアニソール類をアルミナ触媒を用いた
気相中でHFと処理することによりフッ素化する方法
(EP 196,529)。
2. Description of the Related Art The following methods are conventionally known as methods for producing trifluoroanisole. (1) A method of fluorinating trichloroanisole with antimony trifluoride (EP 140,783) or a method of fluorinating with trifluoroanisole (USP 4,876,376). (2) A method of simultaneously performing trichloromethylation and fluorination by reacting phenols with carbon tetrachloride in hydrofluoric acid (USP 4,157,344). (3) A method of fluorinating trichloroanisole by treating it with HF in a gas phase using an alumina catalyst (EP 196,529).

【0003】[0003]

【発明が解決しようとする課題】トリフルオロアニソー
ル類の製造方法として公知の上記の方法には次のような
問題点がある。 (1)のEP140,783 の方法では、トリフルオロアニソ
ール類の収率が充分でない。また、USP4,876,376 の
方法ではトリクロロメトキシ基のフッ素化反応を無水フ
ッ化水素酸中、0℃で実施しているが追試を行ってみた
ところこの反応条件では、ジフルオロ体までしか生成し
ない。 (2)の方法は、170℃でフッ化水素酸を取り扱うた
め、高圧反応となり、危険である。また、反応器の腐蝕
が激しく工業的には問題が多い。 (3)の方法は、気相反応装置が必要であり、触媒寿命
が短い等問題が多い。
The above-mentioned method known as a method for producing trifluoroanisole has the following problems. According to the method of EP140,783 of (1), the yield of trifluoroanisole is not sufficient. Further, in the method of USP 4,876,376, the fluorination reaction of the trichloromethoxy group is carried out in anhydrous hydrofluoric acid at 0 ° C., but when a supplementary test is conducted, only a difluoro body is formed under this reaction condition. The method (2) handles hydrofluoric acid at 170 ° C., so that it is a high-pressure reaction and is dangerous. Further, the reactor is severely corroded, and there are many industrial problems. The method (3) requires a gas phase reaction device and has many problems such as a short catalyst life.

【0004】[0004]

【課題を解決するための手段】本発明は、前述の問題点
を解決すべくなされたものであり、下記化学式(1)で
示されるハロゲン化アニソール類を鉄、アルミニウム、
モリブデン、チタンおよびアンチモンから選ばれる少な
くとも一種の金属のハロゲン化物からなるフッ素化触媒
の存在下、フッ化水素酸と反応させることにより従来法
に比べて温和な反応条件下、高収率で下記一般式(2)
で示されるトリフルオロアニソール類を得る方法を提供
するものである。
The present invention has been made to solve the above-mentioned problems, and halogenated anisole represented by the following chemical formula (1) is added to iron, aluminum,
By reacting with hydrofluoric acid in the presence of a fluorination catalyst composed of a halide of at least one metal selected from molybdenum, titanium and antimony, the following general conditions are used under milder reaction conditions than in conventional methods and in high yields. Formula (2)
The present invention provides a method for obtaining trifluoroanisole represented by

【0005】[0005]

【化3】 [Chemical 3]

【0006】[0006]

【化4】 [Chemical 4]

【0007】式中、Xは塩素原子または臭素原子を示
し、Xが2個以上の場合、Xは同一の原子又は異種の原
子の組み合わせである。R1 ,R2 はハロゲン原子、ア
ルキル基、ハロゲン化アルキル基、アルコキシ基、ホル
ミル基、ハロゲン化ホルミル基、ニトロ基、シアノ基、
カルボキシル基またはカルボアルコキシ基を示し、R1
と同一の位置にあるR2 はR1 と同一の原子または基で
ある。R1 が2個以上の場合、R1 は同一または異種の
原子や基の組合わせであり、R1 と同一の位置にあるR
2 はR1 と同一である。
In the formula, X represents a chlorine atom or a bromine atom, and when X is 2 or more, X is the same atom or a combination of different atoms. R 1 and R 2 are a halogen atom, an alkyl group, a halogenated alkyl group, an alkoxy group, a formyl group, a halogenated formyl group, a nitro group, a cyano group,
R 1 represents a carboxyl group or a carboalkoxy group,
R 2 at the same position as is the same atom or group as R 1 . When R 1 is 2 or more, R 1 is a combination of the same or different atoms or groups, and R 1 is at the same position as R 1.
2 is the same as R 1 .

【0008】ただし、R1 がフッ素原子以外のハロゲン
原子の場合、これと同一の位置にあるR2 はフッ素原子
またはR1 と同一であり、またR1 がフッ素化以外のハ
ロゲン化ホルミル基の場合、これと同一の位置にあるR
2 はフッ素化ホルミル基またはR1 と同一である。nは
1または2、mは0〜5の整数であり、m+n≦6であ
る。pは0〜3、qは0〜2の整数であり、p+q=3
である。
However, when R 1 is a halogen atom other than a fluorine atom, R 2 at the same position as this is the same as a fluorine atom or R 1, and R 1 is a halogenated formyl group other than fluorinated. If R at the same position as
2 is the same as fluorinated formyl group or R 1 . n is 1 or 2, m is an integer of 0 to 5, and m + n ≦ 6. p is an integer of 0 to 3 and q is an integer of 0 to 2, and p + q = 3.
Is.

【0009】前記化学式(1)におけるXが2個以上の
場合、入手が容易であることから塩素原子または臭素原
子の同一原子の組合わせが好ましい。前記化学式(1)
と(2)におけるアルキル基としては炭素数1〜4の低
級アルキル基が好ましい。
When the number of X's in the chemical formula (1) is 2 or more, a combination of the same chlorine atom or bromine atom is preferable because it is easily available. The chemical formula (1)
As the alkyl group in (2), a lower alkyl group having 1 to 4 carbon atoms is preferable.

【0010】前記化学式(1)において、ニトロ基、シ
アノ基、ホルミル基、ハロゲン化ホルミル基等の電子吸
引性基を有しかつ、その基に対してオルトやパラ位にフ
ッ素原子以外のハロゲン原子を有するものは、このハロ
ゲン原子は活性化されており、フッ化水素酸との反応に
よりこのハロゲン原子はフッ素原子に置換されやすい。
例えば、α,α,α,4−テトラクロロ−3−ニトロア
ニソールはフッ化水素酸との反応によりα,α,α,4
−テトラフルオロ−3−ニトロアニソールとなる。
In the above chemical formula (1), the compound has an electron-withdrawing group such as a nitro group, a cyano group, a formyl group and a halogenated formyl group, and has a halogen atom other than a fluorine atom at the ortho or para position with respect to the group. In the case of having a halogen atom, the halogen atom is activated, and the halogen atom is easily substituted with a fluorine atom by the reaction with hydrofluoric acid.
For example, α, α, α, 4-tetrachloro-3-nitroanisole reacts with hydrofluoric acid to produce α, α, α, 4
-Becomes tetrafluoro-3-nitroanisole.

【0011】前記化学式(1)においてフッ素化以外の
ハロゲン化ホルミル基を有するものは、フッ化水素酸と
の反応により、このハロゲン化ホルミル基はフッ素化ホ
ルミル基となりやすい。
In the above chemical formula (1), a compound having a halogenated formyl group other than fluorinated is likely to be a fluorinated formyl group due to a reaction with hydrofluoric acid.

【0012】前記化学式(1)で示される出発原料のハ
ロゲン化アニソール類は比較的入手容易な化合物であ
り、アニソール類を塩素化、臭素化又はフッ素化するこ
とにより合成することができる。
The halogenated anisole of the starting material represented by the chemical formula (1) is a relatively easily available compound, and can be synthesized by chlorinating, brominating or fluorinating the anisole.

【0013】本発明に用いられるフッ化水素酸は好まし
くは無水フッ化水素酸である。フッ化水素酸の使用量は
出発物質のハロゲン化アニソール類に対して3〜100
倍モル、好ましくは3.3〜10倍モルである。フッ素
化触媒の使用量は出発物質のハロゲン化アニソール類に
対して0.01〜100モル%、好ましくは0.1〜1
0モル%である。これらのフッ素化触媒は反応の初期に
添加するかあるいは反応途中のジフルオロ体が生成した
段階で添加してもよい。
The hydrofluoric acid used in the present invention is preferably anhydrous hydrofluoric acid. The amount of hydrofluoric acid used is 3 to 100 relative to the halogenated anisole starting material.
The molar ratio is twice, preferably 3.3 to 10 times. The amount of the fluorination catalyst used is 0.01 to 100 mol%, preferably 0.1 to 1 with respect to the halogenated anisole starting material.
It is 0 mol%. These fluorination catalysts may be added at the initial stage of the reaction, or may be added at the stage where the difluoro compound is formed during the reaction.

【0014】反応温度は−50〜150℃、好ましくは
−10〜50℃であり、液相反応が好ましい。反応温度
が20℃より高いときは、フッ化水素酸が液体となるよ
うに加圧下で行われることが望ましい。反応が進行する
に従い、塩化水素が生成し、圧力が上昇するので還流コ
ンデンサーを通してパージしてもよい。反応時間は出発
物質により異なるが数分から数時間の間である。反応終
了後、蒸留することにより、フッ化水素酸を回収、再使
用することができる。
The reaction temperature is -50 to 150 ° C, preferably -10 to 50 ° C, and liquid phase reaction is preferred. When the reaction temperature is higher than 20 ° C., it is desirable to carry out under pressure so that the hydrofluoric acid becomes a liquid. As the reaction proceeds, hydrogen chloride is produced and the pressure rises, so it may be purged through a reflux condenser. The reaction time varies depending on the starting material, but is between a few minutes and a few hours. After completion of the reaction, the hydrofluoric acid can be recovered and reused by distillation.

【0015】フッ素化触媒としては、鉄、アルミニウ
ム、モリブデン、チタンおよびアンチモンから選ばれる
少なくとも一種の金属のフッ素化物、塩素化物等のハロ
ゲン化物であり、好ましくは五塩化アンチモン等の塩素
化物である。
The fluorination catalyst is a halide of at least one kind of metal selected from iron, aluminum, molybdenum, titanium and antimony, and a halide such as a chloride, preferably a chloride such as antimony pentachloride.

【0016】本発明により合成できる化合物の具体例と
しては、o−クロロ−α,α,α−トリフルオロアニソ
ール、m−クロロ−α,α,α−トリフルオロアニソー
ル、p−クロロ−α,α,α−トリフルオロアニソール
等のハロゲン化トリフルオロアニソール類、4−n−プ
ロピル−α,α,α−トリフルオロアニソール等のアル
キル化トリフルオロアニソール類、4−トリフルオロメ
チル−α,α,α−トリフルオロアニソール等のパーフ
ルオロアルキル化トリフルオロアニソール類、o−ニト
ロ−α,α,α−トリフルオロアニソール、p−ニトロ
−α,α,α−トリフルオロアニソール等のニトロ化ト
リフルオロアニソール類、o−シアノ−α,α,α−ト
リフルオロアニソール、p−シアノ−α,α,α−トリ
フルオロアニソール等のシアノ化トリフルオロアニソー
ル類、4−トリフルオロメトキシベンズアルデヒド、4
−トリフルオロメトキシベンゾイルフルオリド等の化合
物があげられる。
Specific examples of the compound that can be synthesized by the present invention include o-chloro-α, α, α-trifluoroanisole, m-chloro-α, α, α-trifluoroanisole and p-chloro-α, α. , Halogenated trifluoroanisole such as α-trifluoroanisole, alkylated trifluoroanisole such as 4-n-propyl-α, α, α-trifluoroanisole, 4-trifluoromethyl-α, α, α -Perfluoroalkylated trifluoroanisole such as trifluoroanisole, nitrated trifluoroanisole such as o-nitro-α, α, α-trifluoroanisole, p-nitro-α, α, α-trifluoroanisole , O-cyano-α, α, α-trifluoroanisole, p-cyano-α, α, α-trifluoroanisole, etc. Ruoroanisoru acids, 4-trifluoromethoxy benzaldehyde, 4
Examples include compounds such as trifluoromethoxybenzoyl fluoride.

【0017】[0017]

【実施例】【Example】

実施例1 ハステロイ製200mlオートクレーブにα,α,α−
トリクロロアニソール20g(0.0945mol)、
無水フッ化水素酸20g(1.0mol)、五塩化アン
チモン1g(0.003mol)を仕込み、激しく撹拌
しながら15℃で6時間反応を行なった。この時、反応
器の圧力は6kg/cm2 Gまで上昇した。
Example 1 α, α, α-in a Hastelloy 200 ml autoclave
20 g (0.0945 mol) of trichloroanisole,
20 g (1.0 mol) of anhydrous hydrofluoric acid and 1 g (0.003 mol) of antimony pentachloride were charged, and the reaction was carried out at 15 ° C. for 6 hours with vigorous stirring. At this time, the pressure in the reactor rose to 6 kg / cm 2 G.

【0018】反応終了後、ガスクロマトグラフィーで分
析したところ、原料の反応率100%であり、α,α,
α−トリフルオロアニソール以外の生成物は認められな
かった。粗生成物を氷水に投入後、有機層を塩化メチレ
ン抽出および水洗を行った後、蒸留を行い沸点105℃
のα,α,α−トリフルオロアニソール13.3gを得
た。収率86.9%であった。
After completion of the reaction, gas chromatography analysis revealed that the reaction rate of the raw materials was 100%, and α, α,
No products other than α-trifluoroanisole were found. After the crude product was poured into ice water, the organic layer was extracted with methylene chloride and washed with water, and then distilled to have a boiling point of 105 ° C.
There was obtained 13.3 g of α, α, α-trifluoroanisole. The yield was 86.9%.

【0019】実施例2 200mlハステロイC製反応器にα,α,α,3−テ
トラクロロアニソール20g(0.0813mol)、
無水フッ化水素酸40g(2.0mol)を仕込み、0
℃〜20℃まで徐々に昇温しながら反応させた。この時
点での生成物はガスクロ分析の結果、ジフルオロ体のみ
であった。
Example 2 20 g (0.0813 mol) of α, α, α, 3-tetrachloroanisole was added to a 200 ml Hastelloy C reactor.
Charge 40 g (2.0 mol) of anhydrous hydrofluoric acid to 0
The reaction was carried out while gradually increasing the temperature from ℃ to 20 ℃. As a result of gas chromatography analysis, the product at this point was only the difluoro form.

【0020】さらに、五塩化アンチモン1.2g添加
し、同様に0℃から20℃まで昇温しながら6時間反応
を行ったところ、ジフルオロ体が消失し、3−クロロ−
α,α,α−トリフルオロアニソールが生成した。この
時、圧力は6.2kg/cm2Gまで上昇した。実施例
1と同様の処理を行い、3−クロロ−α,α,α−トリ
フルオロアニソール13.6gを得た。収率85.1%
であった。
Furthermore, when 1.2 g of antimony pentachloride was added and the reaction was carried out for 6 hours while raising the temperature from 0 ° C. to 20 ° C., the difluoro compound disappeared and 3-chloro-
α, α, α-trifluoroanisole was produced. At this time, the pressure rose to 6.2 kg / cm 2 G. The same treatment as in Example 1 was carried out to obtain 13.6 g of 3-chloro-α, α, α-trifluoroanisole. Yield 85.1%
Met.

【0021】実施例3 α,α,α,4−テトラクロロアニソールを出発物質と
して用いた以外は実施例2と同様の反応を行い、4−ク
ロロ−α,α,α−トリフルオロアニソール14.4g
を得た。収率90.1%であった。
Example 3 The same reaction as in Example 2 was repeated except that α, α, α, 4-tetrachloroanisole was used as the starting material, and 4-chloro-α, α, α-trifluoroanisole 14. 4 g
Got The yield was 90.1%.

【0022】実施例4 出発物質として4−トリクロロメトキシベンゾイルクロ
リドを用いた以外は実施例2と同様の反応を行い、4−
トリフルオロメトキシベンゾイルフルオリド12.6g
を得た。収率83.1%であった。
Example 4 The same reaction as in Example 2 was repeated except that 4-trichloromethoxybenzoyl chloride was used as the starting material.
Trifluoromethoxybenzoyl fluoride 12.6g
Got The yield was 83.1%.

【0023】比較例1 五塩化アンチモンを添加しない以外は実施例2と同様の
実験を行った。20℃での反応ではジフルオロ体までし
か生成しなかったので徐々に昇温し、70℃で10時間
反応を行ったが反応液をガスクロ分析したところ、トリ
フルオロ体は10%しか生成していなかった。この時圧
力は10kg/cm2 Gまで上昇していた。
Comparative Example 1 The same experiment as in Example 2 was conducted except that antimony pentachloride was not added. In the reaction at 20 ° C, only the difluoro body was formed, so the temperature was gradually raised and the reaction was carried out at 70 ° C for 10 hours. When the reaction solution was analyzed by gas chromatography, only 10% of the trifluoro body was formed. It was At this time, the pressure had risen to 10 kg / cm 2 G.

【0024】比較例2 200mlハステロイ製オートクレーブに三フッ化アン
チモン43.65g(0.24mol)、五塩化アンチ
モン3.65g(0.0122mol)を仕込み、40
℃に保持した。これに4,α,α,α−テトラクロロア
ニソール50g(0.203mol)を滴下した。反応
温度を110℃に上げ、激しく撹拌しながら反応を行っ
た。次いで真空蒸留を行い、4−クロロ−α,α,α−
トリフルオロアニソール19.15gを得た。収率48
%であった。
Comparative Example 2 A 200 ml Hastelloy autoclave was charged with 43.65 g (0.24 mol) of antimony trifluoride and 3.65 g (0.0122 mol) of antimony pentachloride, and 40
Hold at 0 ° C. To this, 50 g (0.203 mol) of 4, α, α, α-tetrachloroanisole was added dropwise. The reaction temperature was raised to 110 ° C., and the reaction was carried out with vigorous stirring. Then, vacuum distillation is carried out, and 4-chloro-α, α, α-
19.15 g of trifluoroanisole was obtained. Yield 48
%Met.

【0025】[0025]

【発明の効果】本発明方法は、従来法に比べ、作業環境
上問題がないとともに、工程数が少なく、安価で収率の
高い優れた方法である。
EFFECTS OF THE INVENTION The method of the present invention is superior to conventional methods in that it has no problems in working environment, has a small number of steps, is inexpensive, and has a high yield.

Claims (1)

【特許請求の範囲】 【請求項1】下記化学式(1)で示されるハロゲン化ア
ニソール類を鉄、アルミニウム、モリブデン、チタンお
よびアンチモンから選ばれる少なくとも一種の金属のハ
ロゲン化物からなるフッ素化触媒の存在下、フッ化水素
酸と反応させることを特徴とする下記化学式(2)で示
されるトリフルオロアニソール類の製造方法。 【化1】 【化2】 式中、Xは塩素原子または臭素原子を示し、Xが2個以
上の場合、Xは同一の原子又は異種の原子の組み合わせ
である。R1 ,R2 はハロゲン原子、アルキル基、ハロ
ゲン化アルキル基、アルコキシ基、ホルミル基、ハロゲ
ン化ホルミル基、ニトロ基、シアノ基、カルボキシル基
またはカルボアルコキシ基を示し、R1と同一の位置に
あるR2 はR1 と同一の原子または基である。R1 が2
個以上の場合、R1 は同一または異種の原子や基の組合
わせであり、R1 と同一の位置にあるR2 はR1 と同一
である。ただし、R1 がフッ素原子以外のハロゲン原子
の場合、これと同一の位置にあるR2 はフッ素原子また
はR1 と同一であり、またR1 がフッ素化以外のハロゲ
ン化ホルミル基の場合、これと同一の位置にあるR2
フッ素化ホルミル基またはR1と同一である。nは1ま
たは2、mは0〜5の整数であり、m+n≦6である。
pは0〜3、qは0〜2の整数であり、p+q=3であ
る。
Claims: 1. The presence of a fluorination catalyst comprising a halogenated anisole represented by the following chemical formula (1) and a halide of at least one metal selected from iron, aluminum, molybdenum, titanium and antimony. A method for producing trifluoroanisole represented by the following chemical formula (2), characterized by reacting with hydrofluoric acid below. [Chemical 1] [Chemical 2] In the formula, X represents a chlorine atom or a bromine atom, and when X is 2 or more, X is the same atom or a combination of different atoms. R 1 and R 2 represent a halogen atom, an alkyl group, a halogenated alkyl group, an alkoxy group, a formyl group, a halogenated formyl group, a nitro group, a cyano group, a carboxyl group or a carboalkoxy group, and at the same position as R 1. Certain R 2 is the same atom or group as R 1 . R 1 is 2
For FOB, R 1 is a combination of same or different atoms or groups, R 2 in the same position and R 1 is the same as R 1. However, when R 1 is a halogen atom other than a fluorine atom, R 2 at the same position as that is the same as a fluorine atom or R 1 , and when R 1 is a halogenated formyl group other than fluorinated, R 2 in the same position as is the same as fluorinated formyl group or R 1 . n is 1 or 2, m is an integer of 0 to 5, and m + n ≦ 6.
p is an integer of 0 to 3, q is an integer of 0 to 2, and p + q = 3.
JP3181851A 1991-06-26 1991-06-26 Production of trifluoroanisole compounds Pending JPH05988A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3181851A JPH05988A (en) 1991-06-26 1991-06-26 Production of trifluoroanisole compounds

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3181851A JPH05988A (en) 1991-06-26 1991-06-26 Production of trifluoroanisole compounds

Publications (1)

Publication Number Publication Date
JPH05988A true JPH05988A (en) 1993-01-08

Family

ID=16107937

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3181851A Pending JPH05988A (en) 1991-06-26 1991-06-26 Production of trifluoroanisole compounds

Country Status (1)

Country Link
JP (1) JPH05988A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6118028A (en) * 1998-03-16 2000-09-12 Occidental Chemical Corporation Method of making trifluoromethoxybenzenes
WO2000075093A1 (en) * 1999-06-07 2000-12-14 Occidental Chemical Corporation METHOD OF MAKING α,α,α-TRIFLUOROMETHOXYBENZENES
WO2001005732A1 (en) * 1999-07-16 2001-01-25 Occidental Chemical Corporation Removal of antimony compounds from liquids

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6118028A (en) * 1998-03-16 2000-09-12 Occidental Chemical Corporation Method of making trifluoromethoxybenzenes
WO2000075093A1 (en) * 1999-06-07 2000-12-14 Occidental Chemical Corporation METHOD OF MAKING α,α,α-TRIFLUOROMETHOXYBENZENES
WO2001005732A1 (en) * 1999-07-16 2001-01-25 Occidental Chemical Corporation Removal of antimony compounds from liquids

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