JPH075493B2 - Process for producing bis (2-hydroxyhexafluoro-2-propyl) benzene derivative - Google Patents

Process for producing bis (2-hydroxyhexafluoro-2-propyl) benzene derivative

Info

Publication number
JPH075493B2
JPH075493B2 JP1162939A JP16293989A JPH075493B2 JP H075493 B2 JPH075493 B2 JP H075493B2 JP 1162939 A JP1162939 A JP 1162939A JP 16293989 A JP16293989 A JP 16293989A JP H075493 B2 JPH075493 B2 JP H075493B2
Authority
JP
Japan
Prior art keywords
reaction
hydroxyhexafluoro
propyl
aluminum chloride
benzene derivative
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.)
Expired - Fee Related
Application number
JP1162939A
Other languages
Japanese (ja)
Other versions
JPH0327338A (en
Inventor
順道 丸田
孝之 西宮
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.)
Central Glass Co Ltd
Original Assignee
Central 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 Central Glass Co Ltd filed Critical Central Glass Co Ltd
Priority to JP1162939A priority Critical patent/JPH075493B2/en
Publication of JPH0327338A publication Critical patent/JPH0327338A/en
Publication of JPH075493B2 publication Critical patent/JPH075493B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

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

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、各種含フッ素ポリマーの原料として有用なビ
ス(2-ヒドロキシヘキサフルオロ‐2-プロピル)ベンゼ
ン誘導体を製造する方法に関する。
TECHNICAL FIELD The present invention relates to a method for producing a bis (2-hydroxyhexafluoro-2-propyl) benzene derivative useful as a raw material for various fluoropolymers.

[従来の技術] 従来、ビス(2-ヒドロキシヘキサフルオロ‐2-プロピ
ル)ベンゼンはヘキサフルオロアセトンを塩化アルミニ
ウムの存在下、ベンゼンと反応させることにより得られ
ることが知られているが[J.Org.Chem.,30,998(196
5)]、上記反応を行う際、ベンゼン(1mol)に塩化ア
ルミニウム(1g)を加え、還流しながら反応温度40〜50
℃を維持し、反応途中で逐次塩化アルミニウムを添加す
るため、合計の塩化アルミニウム使用量は6〜20gとな
り、これはベンゼンに対し4〜15mol%に相当する。
[Prior Art] It is conventionally known that bis (2-hydroxyhexafluoro-2-propyl) benzene can be obtained by reacting hexafluoroacetone with benzene in the presence of aluminum chloride. .Chem., 30,998 (196
5)], When carrying out the above reaction, aluminum chloride (1 g) is added to benzene (1 mol) and the reaction temperature is 40 to 50 while refluxing.
Since the temperature was maintained at 0 ° C. and aluminum chloride was added successively during the reaction, the total amount of aluminum chloride used was 6 to 20 g, which corresponds to 4 to 15 mol% with respect to benzene.

一方、特開昭63−33346号公報においては、ベンゼン780
g(10mol)を二硫化炭素3.5l中に溶解した後、ヘキサフ
ルオロアセトンを3.65kg(22mol)を導入し、さらに塩
化アルミニウムを添加して反応を開始させ、反応温度を
30〜46℃に保つことが記されており、この際塩化アルミ
ニウムは406g(30mol)が消費されている。
On the other hand, in JP-A-63-33346, benzene 780
After dissolving g (10 mol) in 3.5 l of carbon disulfide, 3.65 kg (22 mol) of hexafluoroacetone was introduced, and aluminum chloride was added to start the reaction.
It is stated that the temperature is maintained at 30 to 46 ° C, and at this time, 406g (30mol) of aluminum chloride is consumed.

両者とも反応終了後、水を添加して塩化アルミニウムを
分解し、溶媒を用いて反応生成物を抽出後、蒸留その他
の手法により精製して目的物を得ている。
After completion of the reaction in both cases, water is added to decompose the aluminum chloride, the reaction product is extracted with a solvent, and then purified by distillation or another method to obtain the desired product.

[解決しようとするする課題] 工業的に多量のビス(2-ヒドロキシヘキサフルオロ‐2-
プロピル)ベンゼン誘導体、例えばビス(2-ヒドロキシ
ヘキサフルオロ‐2-プロピル)ベンゼンを製造する方法
として、常圧下での方法は、ヘキサフルオロアセトンの
沸点が−27℃と低いため高価な還流装置を必要とし、密
閉加圧系で行う方法が経済的に有利である。
[Problems to be solved] Industrially large amount of bis (2-hydroxyhexafluoro-2-
Propyl) benzene derivative, for example, bis (2-hydroxyhexafluoro-2-propyl) benzene under normal pressure requires an expensive reflux device because the boiling point of hexafluoroacetone is as low as -27 ° C. It is economically advantageous to use a closed pressure system.

また、ヘキサフルオロアセトンとベンゼン誘導体との反
応を行う場合は、一段目のモノ置換体である(2-ヒドロ
キシヘキサフルオロ‐2-プロピル)ベンゼン誘導体の生
成反応は激しい発熱反応であって、1mol%以下の塩化ア
ルミニウムの存在下において容易に進行するが、二段目
のビス(2-ヒドロキシヘキサフルオロ‐2-プロピル)ベ
ンゼン誘導体の生成反応においては、反応が進行し難
く、上述のように反応が完結するまで塩化アルミニウム
を逐次添加する必要があり、合計量としてはかなり多量
の塩化アルミニウムを使用していた。
When hexafluoroacetone is reacted with a benzene derivative, the production reaction of the first-stage mono-substituted product, (2-hydroxyhexafluoro-2-propyl) benzene derivative, is a violent exothermic reaction at 1 mol%. The reaction proceeds easily in the presence of aluminum chloride below, but in the reaction for producing the bis (2-hydroxyhexafluoro-2-propyl) benzene derivative in the second stage, the reaction is difficult to proceed, and as described above, the reaction It was necessary to add aluminum chloride sequentially until completion, and a considerably large amount of aluminum chloride was used as the total amount.

このように、従来の方法においては、多量の塩化アルミ
ニウムを必要とし、また必要とする塩化アルミニウムの
量の再現性に乏しい等の問題点があり、さらに反応後の
目的生成物を回収する際の問題点としては、従来法では
多量の水により塩化アルミニウムを分解し、塩化メチレ
ン等の抽出溶媒を添加した後相分離し、蒸留精製を行っ
ていたが、ベンゼンを使用した場合は特に、難溶性の結
晶が析出しないように多量の溶媒が必要なこと、界面の
分離が良好でないこと、生成物であるジオールは水の溶
解力が強いため硫酸マグネシウム、硫酸ナトリウム等で
は十分に脱水が行えず、蒸留精製時に水分の混入による
初留損失が大であること等の問題があった。
Thus, in the conventional method, there is a problem that a large amount of aluminum chloride is required and the reproducibility of the required amount of aluminum chloride is poor, and further, when recovering the target product after the reaction, The problem is that in the conventional method, aluminum chloride was decomposed with a large amount of water, phase extraction was performed after adding an extraction solvent such as methylene chloride, and distillation purification was performed. A large amount of solvent is required to prevent the precipitation of crystals, the separation at the interface is not good, and the product diol has a strong water-dissolving power, so that it cannot be dehydrated sufficiently with magnesium sulfate, sodium sulfate, etc. There was a problem that the initial distillation loss due to the mixing of water was large during the distillation purification.

また上述の回収法の問題を避けるため、反応後に直接蒸
留する方法は簡易な方法と考えられるがこの場合高温の
加熱は避けがたく、結果として塩酸の発生とともに、高
沸点副生物を新たに生成するという問題がやはり残る。
Further, in order to avoid the problem of the above-mentioned recovery method, direct distillation after the reaction is considered to be a simple method, but in this case heating at high temperature is unavoidable, and as a result, hydrochloric acid is generated and a high boiling by-product is newly generated. The problem of doing it still remains.

[課題を解決するための手段] 本発明者らはこのような現状において、従来実施されて
いた方法に換え、反応を行う際に十分冷却を行い、温度
を30℃以下の低温に維持したところ、二段目の反応も発
熱的に速やかに進行すること、および反応後の目的生成
物の回収においては、非水系で水酸化ナトリウムのよう
な金属水酸化物での塩化アルミニウムの分解を行ったと
ころ、後の蒸留が良好に行えることを見いだし、本発明
に到達したものである。
[Means for Solving the Problems] Under these circumstances, the present inventors have replaced the conventional method with sufficient cooling when carrying out the reaction and maintaining the temperature at a low temperature of 30 ° C. or lower. In the second step reaction, the reaction proceeded exothermically quickly, and in recovering the target product after the reaction, aluminum chloride was decomposed with a metal hydroxide such as sodium hydroxide in a non-aqueous system. However, they have found that the subsequent distillation can be favorably performed, and have reached the present invention.

すなわち本発明は、一般式 (ただし、式中R1は、水素、ハロゲン、アルキル基の中
から選ばれる基を示す。)で表わされるベンゼン誘導体
に対し、一定量の塩化アルミニウムの存在下、30℃以下
の温度でヘキサフルオロアセトンと反応させた後、アル
カリ金属またはアルカリ土類金属の水酸化物を添加し、
蒸留することを特徴とする一般式 (ただし、R1は前記と同じであり、R2は2-ヒドロキシヘ
キサフルオロ‐2-プロピル基を示す。)で表わされるビ
ス(2-ヒドロキシヘキサフルオロ‐2-プロピル)ベンゼ
ン誘導体の製造法である。
That is, the present invention has the general formula (In the formula, R 1 represents a group selected from hydrogen, halogen and alkyl groups.) Hexafluorofluoride at a temperature of 30 ° C. or lower in the presence of a certain amount of aluminum chloride with respect to the benzene derivative. After reacting with acetone, add hydroxide of alkali metal or alkaline earth metal,
General formula characterized by distillation (However, R 1 is the same as above, and R 2 represents a 2-hydroxyhexafluoro-2-propyl group.) In the process for producing a bis (2-hydroxyhexafluoro-2-propyl) benzene derivative is there.

本発明の製造法において、使用する塩化アルミニウムは
原料のベンゼン誘導体に対し、一定量添加すればよく、
後で逐次添加する必要がない。従って、必要な塩化アル
ミニウムの量は、必要な最低限の量でよく、また再現性
に優れるため、原料のベンゼン誘導体に対しいつも一定
の値を添加すればよい。この場合の塩化アルミニウムの
量は、4〜30mol%が適当である。塩化アルミニウムの
量が4mol%より少ない場合は、反応が十分に進行せず未
反応物が残留する。
In the production method of the present invention, the aluminum chloride to be used may be added in a fixed amount with respect to the raw material benzene derivative,
It is not necessary to add them one after another. Therefore, the required amount of aluminum chloride may be the required minimum amount, and since reproducibility is excellent, a constant value may be added to the benzene derivative as a raw material. In this case, the amount of aluminum chloride is appropriately 4 to 30 mol%. When the amount of aluminum chloride is less than 4 mol%, the reaction does not proceed sufficiently and unreacted substances remain.

一方40mol%より多い場合は、反応は十分に進行する
が、塩化アルミニウムの必要量が多くなり、経済的でな
い。
On the other hand, when it is more than 40 mol%, the reaction proceeds sufficiently, but the required amount of aluminum chloride increases, which is not economical.

反応温度は30℃以下、好ましくは25℃以下であって、無
溶媒系においては原料および生成物の融点より5℃以上
低くない範囲で実施することが好ましい。溶媒を用いる
ことは、生産性の観点から言って好ましくないが、特に
高融点の原料あるいは生成物の場合は、溶媒を用いる方
がよい。この場合、塩化メチレン等の無極性溶媒に溶解
させるのが好ましい。
The reaction temperature is 30 ° C. or lower, preferably 25 ° C. or lower, and in a solventless system, it is preferable to carry out the reaction at a temperature not lower than 5 ° C. or higher than the melting points of the raw materials and the product. The use of a solvent is not preferable from the viewpoint of productivity, but it is preferable to use a solvent particularly in the case of a raw material or product having a high melting point. In this case, it is preferably dissolved in a nonpolar solvent such as methylene chloride.

前記したように、反応は常圧で還流しながら行うことも
できるが、経済的理由からオートクレーブ中で行うほう
が好ましい。
As mentioned above, the reaction can be carried out under reflux at normal pressure, but it is preferable to carry out the reaction in an autoclave for economical reasons.

次に、反応を行った後の目的生成物の回収であるが、触
媒を分解させるために加えるアルカリ金属水酸化物また
はアルカリ土類水酸化物としては、水酸化ナトリウム、
水酸化カリウム、水酸化マグネシウム、水酸化カルシウ
ム等が、例示できる。
Next, for the recovery of the target product after carrying out the reaction, as the alkali metal hydroxide or alkaline earth hydroxide added to decompose the catalyst, sodium hydroxide,
Examples thereof include potassium hydroxide, magnesium hydroxide, calcium hydroxide and the like.

使用量は、用いた塩化アルミニウムに対して等モル量か
ら5倍モル量であり、好ましくは1.5〜3倍モル量であ
る。使用量が等モル量より少ない場合は、未反応の塩化
アルミニウムが残存するため好ましくなく、一方5倍モ
ル量より多い場合は、逆にアルカリが多く残存し、経済
的にも好ましくない。
The amount used is an equimolar amount to 5 times, and preferably 1.5 to 3 times the molar amount of aluminum chloride used. When the amount used is less than the equimolar amount, unreacted aluminum chloride remains, which is not preferable. On the other hand, when the amount is more than 5 times the molar amount, a large amount of alkali remains, which is economically undesirable.

添加方法としては、上記粉末をそのまま反応液に添加す
るか、または極性溶媒に溶解して反応液に添加する。
As an addition method, the above powder is added to the reaction solution as it is, or is dissolved in a polar solvent and added to the reaction solution.

添加により塩化アルミニウムは、水酸化アルミニウムと
上記金属の塩となり、塩酸等を発生せず、また高沸副生
物を与えることなく、容易に蒸留により目的の生成物を
回収することができる。
Upon addition, aluminum chloride becomes a salt of aluminum hydroxide and the above metal, and the desired product can be easily recovered by distillation without generating hydrochloric acid or the like and without giving a high boiling by-product.

[実施例] 以下、実施例により本発明を具体的に説明するが、本発
明は係る実施例に限定されるものではない。
[Examples] Hereinafter, the present invention will be specifically described with reference to Examples, but the present invention is not limited to the Examples.

実施例1 1.6lのオートクレーブにベンゼン234g(3.0mol)と塩化
アルミニウム30gを仕込み、氷浴で反応温度を20〜24℃
に維持しながら、ヘキサフルオロアセトン996gを4時間
要して導入し、さらに15時間反応させた後、ガスクロマ
トグラフィーにより分析したところ、反応率100%、1,3
-ビス(2-ヒドロキシヘキサフルオロ‐2-プロピル)ベ
ンゼンの選択率が82.1%、1,4-ビス(2-ヒドロキシヘキ
サフルオロ‐2-プロピル)ベンゼンの選択率が17.9%で
あった。
Example 1 A 1.6 l autoclave was charged with 234 g (3.0 mol) of benzene and 30 g of aluminum chloride, and the reaction temperature was 20 to 24 ° C. in an ice bath.
Hexafluoroacetone (996 g) was introduced for 4 hours while maintaining the above condition, and after reacting for another 15 hours, gas chromatography analysis revealed that the reaction rate was 100%, 1,3
The selectivity of -bis (2-hydroxyhexafluoro-2-propyl) benzene was 82.1% and the selectivity of 1,4-bis (2-hydroxyhexafluoro-2-propyl) benzene was 17.9%.

実施例2 実施例1で得た反応溶液に水酸化ナトリウム28g(0.7mo
l、使用した塩化アルミニウムに対して3.1倍モル量)を
添加、攪拌し、そのまま減圧蒸留(102〜108℃/18〜20m
mHg)して、1066.4gの生成物を回収した。この場合の回
収率は86.7%であり、回収液中の1,3-ビス(2-ヒドロキ
シヘキサフルオロ‐2-プロピル)ベンゼンは83.8%、1,
4-ビス(2-ヒドロキシヘキサフルオロ‐2-プロピル)ベ
ンゼンは16.2%であった。
Example 2 28 g (0.7 mol) of sodium hydroxide was added to the reaction solution obtained in Example 1.
l, 3.1 times the molar amount of aluminum chloride used), stir and distill under reduced pressure (102-108 ℃ / 18-20m)
mHg) and 1066.4 g of product was recovered. The recovery rate in this case was 86.7%, and 1,3-bis (2-hydroxyhexafluoro-2-propyl) benzene in the recovered solution was 83.8%,
4-bis (2-hydroxyhexafluoro-2-propyl) benzene was 16.2%.

実施例3 1のオートクレーブに、フルオロベンゼン192g(2mo
l)、塩化アルミニウム80g(30mol%)を仕込み、氷浴
で冷却して25〜30℃に維持しながら、ヘキサフルオロア
セトン708gを8時間要して仕込み、更に16時間反応させ
た後、ガスクロマトグラフィーにより分析したところ、
反応率100%、2,4-ビス(2-ヒドロキシヘキサフルオロ
‐2-プロピル)フルオロベンゼンの選択率が100%であ
った。
Example 3 In the autoclave of 1, 192 g of fluorobenzene (2mo
l), 80 g (30 mol%) of aluminum chloride were charged, 708 g of hexafluoroacetone was added for 8 hours while cooling with an ice bath and maintaining at 25 to 30 ° C, and after reacting for 16 hours, gas chromatography was performed. When analyzed by graphy,
The reaction rate was 100%, and the selectivity of 2,4-bis (2-hydroxyhexafluoro-2-propyl) fluorobenzene was 100%.

実施例4 実施例3で得た反応溶液に水酸化カリウム105g(1.88mo
l、使用した塩化アルミニウムに対して3.1倍モル量)を
添加、攪拌し、そのまま減圧蒸留(97〜98℃/16mmHg)
して、761gの生成物を回収した。この場合の回収率は8
8.4%であり、回収液中の2,4-ビス(2-ヒドロキシヘキ
サフルオロ‐2-プロピル)フルオロベンゼンの純度は9
9.9%であった。
Example 4 105 g of potassium hydroxide (1.88 mol) was added to the reaction solution obtained in Example 3.
l, 3.1 times the molar amount of aluminum chloride used), stirred and vacuum distilled as it is (97-98 ° C / 16mmHg)
Recovery, 761 g of product was recovered. The recovery rate in this case is 8
8.4%, and the purity of 2,4-bis (2-hydroxyhexafluoro-2-propyl) fluorobenzene in the recovered liquid was 9
It was 9.9%.

[発明の効果] 本発明の製造法によれば、反応温度を30℃以下に維持す
ることにより、触媒の塩化アルミニウムを、最低限必要
な量だけ添加することにより、再現性よく反応が迅速に
進行し、その後の反応生成物の回収も、蒸留により容易
にかつ効率よく行うことができ、工業的に極めて有利な
方法である。
[Effects of the Invention] According to the production method of the present invention, the reaction temperature is maintained at 30 ° C or lower, and the minimum necessary amount of aluminum chloride as a catalyst is added, so that the reaction can be performed rapidly with good reproducibility. The progress of the reaction product and the subsequent recovery of the reaction product can be carried out easily and efficiently by distillation, which is an industrially extremely advantageous method.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】一般式 (ただし、式中R1は、水素、ハロゲン、アルキル基の中
から選ばれる基を示す。)で表わされるベンゼン誘導体
に対し、一定量の塩化アルミニウムの存在下、30℃以下
の温度でヘキサフルオロアセトンと反応させた後、アル
カリ金属またはアルカリ土類金属の水酸化物を添加し、
蒸留することを特徴とする一般式 (ただし、R1は前記と同じであり、R2は2-ヒドロキシヘ
キサフルオロ‐2-プロピル基を示す。)で表わされるビ
ス(2-ヒドロキシヘキサフルオロ‐2-プロピル)ベンゼ
ン誘導体の製造法。
1. A general formula (In the formula, R 1 represents a group selected from hydrogen, halogen and alkyl groups.) Hexafluorofluoride at a temperature of 30 ° C. or lower in the presence of a certain amount of aluminum chloride with respect to the benzene derivative. After reacting with acetone, add hydroxide of alkali metal or alkaline earth metal,
General formula characterized by distillation (However, R 1 is the same as the above, and R 2 represents a 2-hydroxyhexafluoro-2-propyl group.) A method for producing a bis (2-hydroxyhexafluoro-2-propyl) benzene derivative represented by the following.
JP1162939A 1989-06-26 1989-06-26 Process for producing bis (2-hydroxyhexafluoro-2-propyl) benzene derivative Expired - Fee Related JPH075493B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1162939A JPH075493B2 (en) 1989-06-26 1989-06-26 Process for producing bis (2-hydroxyhexafluoro-2-propyl) benzene derivative

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1162939A JPH075493B2 (en) 1989-06-26 1989-06-26 Process for producing bis (2-hydroxyhexafluoro-2-propyl) benzene derivative

Publications (2)

Publication Number Publication Date
JPH0327338A JPH0327338A (en) 1991-02-05
JPH075493B2 true JPH075493B2 (en) 1995-01-25

Family

ID=15764122

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1162939A Expired - Fee Related JPH075493B2 (en) 1989-06-26 1989-06-26 Process for producing bis (2-hydroxyhexafluoro-2-propyl) benzene derivative

Country Status (1)

Country Link
JP (1) JPH075493B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1300076C (en) * 2005-08-05 2007-02-14 上海康鹏化学有限公司 Preparation method of double(2-hydroxyl hexafluopropyl) phenol

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115140872A (en) * 2022-09-07 2022-10-04 中山市中环环保废液回收有限公司 Low-energy-consumption treatment method for high-salt high-COD wastewater

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3624911A1 (en) * 1986-07-23 1988-01-28 Hoechst Ag METHOD FOR SEPARATING ISOMERIC MIXTURES FROM 1.3- AND 1.4-BIS- (2-HYDROXYHEXAFLUORO-2-PROPYL) -BENZOLE

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1300076C (en) * 2005-08-05 2007-02-14 上海康鹏化学有限公司 Preparation method of double(2-hydroxyl hexafluopropyl) phenol

Also Published As

Publication number Publication date
JPH0327338A (en) 1991-02-05

Similar Documents

Publication Publication Date Title
JP2911626B2 (en) Preparation of carboxylic acid chloride
WO1994024086A1 (en) Process for producing 2-fluoroisobutyric acid or ester thereof
JP3337728B2 (en) Method for producing 2-acetylbenzo [b] thiophene
JPH075493B2 (en) Process for producing bis (2-hydroxyhexafluoro-2-propyl) benzene derivative
EP0101625B1 (en) Process for preparing the 2',4'-difluoro-4-hydroxy-(1,1'-diphenyl)-3-carboxylic acid
JPS6312048B2 (en)
EP1468983B1 (en) Process for producing 2,5-bis(trifluoromethyl)nitrobenzene
JPS629098B2 (en)
JPS6354331A (en) Production of 1,1-difluorocyclohexane
JPH08231462A (en) Perfluoroalkylarboxylic acid fluoride and production of its derivative
EP0132990B1 (en) Production of hexanitrostilbene (hns)
JP4665306B2 (en) Method for producing fluorinated alkylamine compound
KR0129408B1 (en) Process for preparation of 1-hydroxycyclohexylphenyl ketone
JPH1112204A (en) 9,10-dichloroanthracene compounds and production of 9,10-dihaloanthracene compounds
JP3760253B2 (en) Process for producing 4-fluorosalicylic acids
JP2937330B2 (en) Bis (2,3,5,6-tetrafluoro-4-aminophenyl) methane
WO2021240331A1 (en) Process for the preparation of 3,5-dichloro-2,2,2-trifluoroacetophenone
JPH0717547B2 (en) Method for producing 1,1-difluorocyclohexane
JP2008247746A (en) Method for producing haloiodoaniline compounds
JPH045657B2 (en)
JPS6348234A (en) Production of 2,5-di(chloromethyl)-p-xylene
JP2649722B2 (en) Method for producing 4,4 '-(1-phenylethylidene) bisphenol
JPH0582380B2 (en)
JPH0456815B2 (en)
WO1999058488A1 (en) Improved process for the preparation of trifluoromethyl containing derivatives

Legal Events

Date Code Title Description
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080125

Year of fee payment: 13

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090125

Year of fee payment: 14

LAPS Cancellation because of no payment of annual fees