JPH09110785A - Production of phthalic acid derivative - Google Patents

Production of phthalic acid derivative

Info

Publication number
JPH09110785A
JPH09110785A JP26600795A JP26600795A JPH09110785A JP H09110785 A JPH09110785 A JP H09110785A JP 26600795 A JP26600795 A JP 26600795A JP 26600795 A JP26600795 A JP 26600795A JP H09110785 A JPH09110785 A JP H09110785A
Authority
JP
Japan
Prior art keywords
product
reaction
added
tetrafluorobenzene
bis
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.)
Granted
Application number
JP26600795A
Other languages
Japanese (ja)
Other versions
JP3739119B2 (en
Inventor
Yasunori Okumura
康則 奥村
Koji Yoshitoshi
孝司 吉年
Osamu Kaieda
修 海江田
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.)
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 JP26600795A priority Critical patent/JP3739119B2/en
Publication of JPH09110785A publication Critical patent/JPH09110785A/en
Application granted granted Critical
Publication of JP3739119B2 publication Critical patent/JP3739119B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To industrially obtain in high purity and yield a phthalic acid derivative useful as an intermediate for polyimides, by heating a specific phthalonitrile derivative under an acidic condition to form a reaction product which is then dissolved in a specific medium and separated, and by heating the product in an acidic medium and then separating the product. SOLUTION: First, a compound of formula I (X is a halogen) such as 1,4-bis(3,4-dicyanotrifluorophenoxy)tetrafluorobenzene is heated in an acidic aqueous medium to form a product containing a compound A of formula II such as 1,4-bis(3,4-dicarboxytrifluorophenoxy)tetrafluorobenzene. Subsequently, the product is once dissolved in an medium containing an organic solvent (e.g. containing at least 50wt.% of a ketone) and then separated, and the product is, in turn, heated in an acidic aqueous medium; the above process is repeated, and, finally, the product containing the compound A is separated from the acidic medium.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、下記一般式(II)
で表わされるフタル酸誘導体の製造方法に関するもので
ある。
TECHNICAL FIELD The present invention relates to the following general formula (II)
The present invention relates to a method for producing a phthalic acid derivative represented by

【0002】本発明にかかるフタル酸誘導体は、光学材
料、配線基板材料、感光材料、液晶材料などの中間原料
として有用である。特に、光学材料、配線基板材料とし
て用いられるポリイミドの中間体として有用である。
The phthalic acid derivative according to the present invention is useful as an intermediate raw material for optical materials, wiring board materials, photosensitive materials, liquid crystal materials and the like. In particular, it is useful as an intermediate of polyimide used as an optical material or a wiring board material.

【0003】[0003]

【従来の技術】従来、フタル酸誘導体としては、例え
ば、1,4−ビス(3,4−ジカルボキシトリフルオロ
フェノキシ)テトラフルオロベンゼンの製造方法につい
て特開平5−1148号に、1,4−ビス(3,4−ジ
シアノトリフルオロフェノキシ)テトラフルオロベンゼ
ンを60%硫酸水溶液中150℃で15時間反応する方
法が開示されている。しかしながら、後記の参考例1か
らわかるようにこの方法では、その純度が95%未満の
ものしか得られず、実用的な材料としては問題を有して
いる。
2. Description of the Related Art Conventionally, as a phthalic acid derivative, for example, a method for producing 1,4-bis (3,4-dicarboxytrifluorophenoxy) tetrafluorobenzene is disclosed in JP-A-5-1148. A method of reacting bis (3,4-dicyanotrifluorophenoxy) tetrafluorobenzene in a 60% sulfuric acid aqueous solution at 150 ° C. for 15 hours is disclosed. However, as can be seen from Reference Example 1 described below, this method has a problem that the purity is less than 95%, which is a practical material.

【0004】[0004]

【発明が解決しようとする課題】本発明の目的は、フタ
ル酸誘導体を工業的に可能で、かつ高収率な方法で高純
度のフタル酸誘導体を得ることのできる製造方法を提供
することにある。
DISCLOSURE OF THE INVENTION An object of the present invention is to provide a method for producing a phthalic acid derivative industrially and capable of obtaining a highly pure phthalic acid derivative with a high yield. is there.

【0005】[0005]

【課題を解決するための手段】本発明者らは、下記一般
式(I)で表わされるフタロニトリル誘導体の加水分解
反応により得られるフタル酸誘導体の製造方法について
鋭意検討を行った結果、フタル酸誘導体の純度を低下さ
せている原因が何かを突き止め、その対策方法を見いだ
し本発明を完成するに至った。
Means for Solving the Problems The inventors of the present invention have earnestly studied a method for producing a phthalic acid derivative obtained by a hydrolysis reaction of a phthalonitrile derivative represented by the following general formula (I). The cause of the decrease in the purity of the derivative was identified, a countermeasure against the problem was found, and the present invention was completed.

【0006】まず、純度を低下させている原因が何かを
突き止めるため、硫酸水溶液での加水分解反応の分析を
行った。その結果、フタロニトリル誘導体の加水分解に
おける反応中間体のフタルアミド誘導体などが、かなり
生成物中に残存していることがわかった。その反応中間
体のフタルアミド誘導体などが残存する理由について説
明する。まず、加水分解反応の反応形態は、フタリニト
リル誘導体が固体で分散している硫酸水溶液を加熱し、
徐々にフタロニトリル誘導体がとけて,有機相、水相の
二相状態で反応が進行する。その後、反応の進行と共に
反応中間体のフタルアミド誘導体などあるいは目的物の
フタル酸誘導体が析出してくる。その際水溶液と接触し
ているフタルアミド誘導体などは、さらに反応が進行し
目的物のフタル酸誘導体となるが、フタル酸誘導体の内
部に取り込まれて水溶液と接触していないフタルアミド
誘導体はそれ以上反応が進行しなくなる。そのためフタ
ル酸誘導体の純度が低下してしまう結果となった。
First, in order to find out what is causing the decrease in purity, the hydrolysis reaction in an aqueous sulfuric acid solution was analyzed. As a result, it was found that a phthalamide derivative, which is a reaction intermediate in the hydrolysis of the phthalonitrile derivative, remained in the product considerably. The reason why the reaction intermediate such as a phthalamide derivative remains will be described. First, the reaction form of the hydrolysis reaction is as follows: Heating the sulfuric acid aqueous solution in which the phthalinitrile derivative is dispersed as a solid,
The phthalonitrile derivative gradually melts, and the reaction proceeds in a two-phase state of an organic phase and an aqueous phase. Thereafter, as the reaction progresses, a phthalamide derivative as a reaction intermediate or a target phthalic acid derivative is deposited. At that time, the phthalamide derivative or the like that is in contact with the aqueous solution is further reacted and becomes the target phthalic acid derivative, but the phthalamide derivative that is taken inside the phthalic acid derivative and is not in contact with the aqueous solution is further reacted. It will not progress. As a result, the purity of the phthalic acid derivative was reduced.

【0007】そこで、本発明者らは、その製造方法とし
て、生成物を一旦溶解した後析出させ取り出すことで、
内部に取り込まれたフタルアミド誘導体を固体表面に析
出させ、その後さらに加水分解することによりフタル酸
誘導体とすることで、純度の向上を行うことを検討した
結果、下記に示す製造方法を完成した。
Therefore, the inventors of the present invention, as a method for producing the same, by once dissolving the product and then depositing and taking it out,
As a result of investigating improving the purity by precipitating the phthalamide derivative taken in on the solid surface and then further hydrolyzing it to obtain a phthalic acid derivative, the following production method was completed.

【0008】すなわち、本発明の目的は、(1)
(イ)下記一般式(I)で表わされる化合物を酸性水媒
体中で加熱し、下記一般式(II)で表わされる化合物を
含有する生成物を得、(ロ)次いで、得られた生成物を
有機溶媒を含有する媒体中に一旦溶解し、(ハ)媒体中
より生成物を分離し、(ニ)さらに、得られた生成物を
酸性水媒体中で加熱し、(ホ)その後、得られた酸性水
媒体中から生成物を分離する、とする工程において、上
記(イ)〜(ニ)の工程を行った後、(ロ)〜(ニ)の
工程を少なくとも1回以上繰り返し行い、最後に(ホ)
の工程を行って下記一般式(II)で表わされるフタル酸
誘導体を含有する生成物を得ることを特徴とする製造方
法により達成される。
That is, the object of the present invention is (1)
(A) A compound represented by the following general formula (I) is heated in an acidic aqueous medium to obtain a product containing the compound represented by the following general formula (II), and (b) the obtained product. Is once dissolved in a medium containing an organic solvent, (c) the product is separated from the medium, (d) the product obtained is heated in an acidic aqueous medium, and (e) after that, In the step of separating the product from the obtained acidic aqueous medium, after performing the steps (a) to (d), the steps (b) to (d) are repeated at least once or more, Finally (e)
Is carried out to obtain a product containing a phthalic acid derivative represented by the following general formula (II).

【0009】[0009]

【化3】 Embedded image

【0010】[0010]

【化4】 Embedded image

【0011】また、本発明の他の目的は、(2) 前記
一般式(I)の化合物が、1,4−ビス(3,4−ジシ
アノトリフルオロフェノキシ)テトラフルオロベンゼン
であり、前記一般式(II)の化合物が、1,4−ビス
(3,4−ジカルボキシトリフルオロフェノキシ)テト
ラフルオロベンゼンである上記(1)に示す製造方法に
よっても達成される。
Another object of the present invention is (2) wherein the compound of the general formula (I) is 1,4-bis (3,4-dicyanotrifluorophenoxy) tetrafluorobenzene, It is also achieved by the production method described in (1) above, wherein the compound (II) is 1,4-bis (3,4-dicarboxytrifluorophenoxy) tetrafluorobenzene.

【0012】さらに、本発明の他の目的は、(3) 前
記(ロ)の工程の有機溶媒を含有する媒体が、少なくと
も50%重量以上のケトン類を含有することを特徴とす
る上記(1)または(2)に示す製造方法によっても達
成される。
Further, another object of the present invention is (3), wherein the medium containing the organic solvent in the step (b) contains at least 50% by weight or more of ketones. ) Or (2).

【0013】[0013]

【発明の実施の形態】本発明につき、それぞれの工程に
ついて詳しく説明する。
DETAILED DESCRIPTION OF THE INVENTION Each step of the present invention will be described in detail.

【0014】(1) 工程(イ)について この工程は、上記一般式(I)で表されるフタロニトリ
ル誘導体(以下、単にフタロニトリル誘導体ともいう)
を酸性条件で加水分解し、上記一般式(II)で表される
フタル酸誘導体(以下、単にフタル酸誘導体ともいう)
を含有する生成物を得る工程である。
(1) Step (a) In this step, the phthalonitrile derivative represented by the above general formula (I) (hereinafter, also simply referred to as phthalonitrile derivative).
Is hydrolyzed under acidic conditions to give a phthalic acid derivative represented by the above general formula (II) (hereinafter also simply referred to as a phthalic acid derivative)
Is a step of obtaining a product containing

【0015】本工程では、通常80%以上のフタル酸誘
導体を含有する生成物を得るように反応を行うが、好ま
しくは87%以上のフタル酸誘導体を含有する生成物を
得るように反応を行う。
In this step, the reaction is usually carried out so as to obtain a product containing 80% or more phthalic acid derivative, but preferably the reaction is carried out so as to obtain a product containing 87% or more phthalic acid derivative. .

【0016】反応の形態は、反応開始時にフタロニトリ
ル誘導体と酸性水媒体を一括で投入した後に所定時間反
応を行っても良いし、反応中に酸性水媒体中にフタロニ
トリル誘導体を数回に分割して投入しても良い。分割し
て投入する場合の投入方法としては、粉体のままで行っ
ても良いし、例えば、無水酢酸、無水プロピオン酸、ア
セトニトリル等の溶媒に溶解させて行っても良い。
The reaction may be carried out by adding the phthalonitrile derivative and the acidic aqueous medium together at the start of the reaction, and then performing the reaction for a predetermined period of time, or dividing the phthalonitrile derivative into the acidic aqueous medium several times during the reaction. Then you can throw it in. As the charging method in the case of dividing and charging, the powder may be used as it is, or may be dissolved in a solvent such as acetic anhydride, propionic anhydride, or acetonitrile, for example.

【0017】本工程で使用される酸性水媒体としては、
例えば、リン酸水溶液、硫酸水溶液、塩酸水溶液などの
無機酸水溶液を用いて反応を行うことが好ましく、特に
硫酸水溶液が好ましい。硫酸水溶液を用いることで、効
率よく高収率で目的物を得ることができる。
As the acidic aqueous medium used in this step,
For example, it is preferable to carry out the reaction using an aqueous solution of an inorganic acid such as an aqueous solution of phosphoric acid, an aqueous solution of sulfuric acid, an aqueous solution of hydrochloric acid, and an aqueous solution of sulfuric acid is particularly preferred. By using the sulfuric acid aqueous solution, the target product can be efficiently obtained in a high yield.

【0018】例えば、反応に硫酸水溶液を用いた場合に
ついて詳しく説明する。
For example, the case of using a sulfuric acid aqueous solution for the reaction will be described in detail.

【0019】まず、本工程における硫酸の濃度は、40
〜85重量%の範囲の硫酸水溶液を用いることが好まし
く、特に50〜80重量%の範囲の硫酸水溶液を用いる
ことが好ましい。硫酸の濃度が、高い場合には反応中間
体のアミドあるいはフタル酸誘導体の無水物などが生成
し易くなり純度が低下することや、反応終了後硫酸を除
去することが困難になる。また、低い場合には反応温度
を十分に上げられなくなり反応速度が低下し生産性が悪
くなってしまう。
First, the concentration of sulfuric acid in this step is 40
It is preferable to use an aqueous solution of sulfuric acid in the range of to 85% by weight, and particularly preferable to use an aqueous solution of sulfuric acid in the range of 50 to 80% by weight. When the concentration of sulfuric acid is high, the reaction intermediate such as amide or anhydride of phthalic acid derivative is likely to be produced and the purity is lowered, and it is difficult to remove the sulfuric acid after the reaction. On the other hand, if it is low, the reaction temperature cannot be raised sufficiently and the reaction rate decreases, resulting in poor productivity.

【0020】本工程において、フタロニトリル誘導体の
硫酸水溶液に対する濃度は、5〜50重量%の範囲の濃
度で行うことが好ましい。濃度が高い場合には、反応の
制御が困難になり、低い場合には生産性が悪くなってし
まい好ましくない。
In this step, the concentration of the phthalonitrile derivative in the aqueous sulfuric acid solution is preferably in the range of 5 to 50% by weight. When the concentration is high, it becomes difficult to control the reaction, and when the concentration is low, productivity is deteriorated, which is not preferable.

【0021】また、本工程における反応温度は、120
〜180℃の範囲で行うことが好ましく、特に140〜
170℃の範囲で行うことが好ましい。反応温度が高い
場合には、反応の制御が困難になり、低い場合には反応
速度が低下し生産性が悪くなってしい好ましくない。
The reaction temperature in this step is 120.
It is preferable to carry out in the range of ~ 180 ° C, especially 140 ~
It is preferably carried out in the range of 170 ° C. When the reaction temperature is high, it becomes difficult to control the reaction, and when the reaction temperature is low, the reaction rate decreases and the productivity deteriorates, which is not preferable.

【0022】本工程における反応時間は、反応温度など
によるが通常1〜24時間で行うことができる。
The reaction time in this step depends on the reaction temperature and the like, but can be usually 1 to 24 hours.

【0023】反応終了後、反応液中に生成物のフタル酸
誘導体が析出してくるが、次工程(ロ)に用いる時、反
応液をそのまま用いても良いし、濾過し濾物のみを用い
ても良い。
After completion of the reaction, the phthalic acid derivative as a product is precipitated in the reaction solution. When using in the next step (b), the reaction solution may be used as it is or may be filtered to use only the filtered material. May be.

【0024】工程(ロ)、(ハ)について これらの工程は、前工程(イ)で得られた生成物また
は、工程(ニ)で得られた反応液を有機溶媒を含有する
媒体中に一旦溶解し(工程(ロ))、媒体中より生成物
を分離する(工程(ハ))ことで、フタル酸誘導体の内
部に取り込まれたフタルアミド誘導体などを固体の表面
に出させる工程である。
Regarding Steps (b) and (c) In these steps, the product obtained in the previous step (a) or the reaction solution obtained in the step (d) is once added to a medium containing an organic solvent. By dissolving (step (b)) and separating the product from the medium (step (c)), the phthalamide derivative and the like incorporated inside the phthalic acid derivative are exposed on the solid surface.

【0025】本工程では、その方法として、工程(イ)
の反応溶液に直接水と2層状態になる有機溶媒を加え生
成物を溶解させ(工程(ロ))、その後有機層を分液し
蒸発乾固する(工程(ハ))方法がある。
In this step, the method is as follows:
There is a method in which water and an organic solvent having a two-layered state are directly added to the reaction solution of (3) to dissolve the product (step (b)), and then the organic layer is separated and evaporated to dryness (step (c)).

【0026】加える有機溶媒としては、水と2層状態に
なり、生成物と反応しないものであれば特に限定される
ものではないが、脂肪酸エステル類、ケトン類、エーテ
ル類、ベンゾニトリル類が好ましく、特に脂肪酸エステ
ル類、ケトン類が好ましい。例えば、酢酸エチル、酢酸
イソプロピル、メチルイソブチルケトンなどが挙げられ
る。使用する有機溶媒の量は、生成物を溶解し得る量以
上であれば問題ない。その後、媒体中より有機層を分液
し、必要であれば有機層を水洗してもよい。その後、蒸
発乾固し生成物を得、次工程(ニ)に使用する。
The organic solvent to be added is not particularly limited as long as it has a two-layer state with water and does not react with the product, but fatty acid esters, ketones, ethers and benzonitriles are preferable. Especially, fatty acid esters and ketones are preferable. Examples thereof include ethyl acetate, isopropyl acetate, methyl isobutyl ketone and the like. There is no problem with the amount of the organic solvent used as long as it can dissolve the product. After that, the organic layer may be separated from the medium, and the organic layer may be washed with water if necessary. Then, it is evaporated to dryness to obtain a product, which is used in the next step (d).

【0027】本工程(ロ)、(ハ)では、また別の方法
として、工程(イ)の反応溶液を一旦瀘過し得られた瀘
物に有機溶媒を含有する媒体を加え溶解させ(工程
(ロ))、その後加えた有機溶媒が水と2層状態になる
ものであれば分液し、有機層を蒸発乾固することで生成
物を得、加えた有機溶媒が水と2層状態にならないもの
であれば水を固体が析出するまでその後加え瀘過、乾燥
により生成物を得る(工程(ハ))ことができる。
In the present steps (b) and (c), as another method, the reaction solution of the step (a) is once filtered, and a medium containing an organic solvent is added to and dissolved in the filtrate (step (B)), if the organic solvent added thereafter is in a two-layer state with water, liquid separation is performed, and the product is obtained by evaporating the organic layer to dryness, and the added organic solvent is in a two-layer state with water. If it does not become, the product can be obtained by adding water thereafter until a solid is precipitated and then filtering and drying (step (c)).

【0028】水と2層状態になる有機溶媒を用いる場
合、加える有機溶媒としては、生成物と反応しないもの
であれば特に制限されるものでないが、脂肪酸エステル
類、ケトン類、エーテル類、ベンゾニトリル類が好まし
く、特に脂肪酸エステル類、ケトン類が好ましい。例え
ば、酢酸エチル、酢酸イソプロピル、メチルイソブチル
ケトンなどが挙げられる。使用する有機溶媒の量は、生
成物を溶解し得る量以上であれば問題はない。その後、
有機層を分液し、必要であれば有機層を水洗してもよ
い。その後、有機層を蒸発乾固し生成物を得、次工程
(ニ)に使用する。
When an organic solvent having a two-layer state with water is used, the organic solvent to be added is not particularly limited as long as it does not react with the product, but fatty acid esters, ketones, ethers, benzo Nitriles are preferable, and fatty acid esters and ketones are particularly preferable. Examples thereof include ethyl acetate, isopropyl acetate, methyl isobutyl ketone and the like. There is no problem as long as the amount of the organic solvent used is at least an amount capable of dissolving the product. afterwards,
The organic layer may be separated, and if necessary, the organic layer may be washed with water. Then, the organic layer is evaporated to dryness to obtain a product, which is used in the next step (d).

【0029】水と2層状態ならないものを用いる場合、
加える有機溶媒としては、生成物と反応しないものであ
れば特に限定されるものではないが、ケトン類、アセト
ニトリル類、アルコール類が好ましく、特にケトン類が
好ましい。例えば、アセトン、アセトニトリル、メタノ
ール、エタノールなどが挙げられる。使用する有機溶媒
の量は、生成物を溶解し得る量以上であれば問題ない。
その後、水を固体が析出するまで加え、瀘過、乾燥によ
り生成物を得、次工程(ニ)に使用する。
When using a material that does not form a two-layer state with water,
The organic solvent to be added is not particularly limited as long as it does not react with the product, but ketones, acetonitriles and alcohols are preferable, and ketones are particularly preferable. For example, acetone, acetonitrile, methanol, ethanol and the like can be mentioned. There is no problem with the amount of the organic solvent used as long as it can dissolve the product.
Then, water is added until a solid precipitates, and the product is obtained by filtration and drying and used in the next step (d).

【0030】水の量は、固体が析出する量以上加えれば
問題ないが、例えば、有機溶媒がアセトンの場合、重量
で5倍以上の水を用いればよい。
There is no problem as long as the amount of water is added in such an amount that solids are deposited. For example, when the organic solvent is acetone, water may be used in an amount 5 times or more by weight.

【0031】(3) 工程(ニ)について この工程は、工程(ハ)で得られた生成物をさらに加水
分解する工程である。
(3) Step (d) This step is a step of further hydrolyzing the product obtained in step (c).

【0032】反応の形態は、反応開始時に工程(ハ)で
得られた生成物と酸性水媒体を一括で投入した後に所定
時間反応を行ってもよいし、反応器中の酸性水媒体中に
工程(ハ)で得られた生成物を数回に分割して投入して
も良い。分割して投入する場合の投入方法としては、粉
体のままで行っても良いし、例えば、無水酢酸、無水プ
ロピオン酸、アセトニトリルなどの溶媒に溶解させて行
っても良い。
The reaction may be carried out by adding the product obtained in step (c) and the acidic aqueous medium together at the start of the reaction, and then performing the reaction for a predetermined time. Alternatively, the reaction may be performed in the acidic aqueous medium in the reactor. The product obtained in step (c) may be divided and added several times. As a charging method in the case of dividing and charging, the powder may be used as it is, or may be dissolved in a solvent such as acetic anhydride, propionic anhydride, or acetonitrile, for example.

【0033】本工程に使用される酸性水媒体としては、
リン酸水溶液、硫酸水溶液、塩酸水溶液などの無機酸水
溶液を用いて反応を行うことが好ましく、特に硫酸水溶
液が好ましい。硫酸水溶液を用いることで、効率よく高
収率で目的物を得ることができる。
As the acidic aqueous medium used in this step,
The reaction is preferably carried out using an aqueous solution of an inorganic acid such as an aqueous solution of phosphoric acid, an aqueous solution of sulfuric acid, an aqueous solution of hydrochloric acid, and an aqueous solution of sulfuric acid is particularly preferred. By using the sulfuric acid aqueous solution, the target product can be efficiently obtained in a high yield.

【0034】例えば、反応に硫酸水溶液を用いる場合に
ついて詳しく説明する。
For example, the case of using a sulfuric acid aqueous solution for the reaction will be described in detail.

【0035】まず、本工程における硫酸の濃度は、40
〜85重量%の範囲の硫酸水溶液を用いることが好まし
く、特に50〜80重量%の範囲の硫酸水溶液を用いる
ことが好ましい。硫酸の濃度が、高い場合には反応中間
体のアミドあるいはフタル酸誘導体の無水物などが生成
し易くなり純度が低下することや、反応終了後硫酸を除
去することが困難になる。また、低い場合には反応温度
を十分に上げられなくなり反応速度が低下し生産性が悪
くなってしまう。
First, the concentration of sulfuric acid in this step is 40
It is preferable to use an aqueous solution of sulfuric acid in the range of to 85% by weight, and particularly preferable to use an aqueous solution of sulfuric acid in the range of 50 to 80% by weight. When the concentration of sulfuric acid is high, the reaction intermediate such as amide or anhydride of phthalic acid derivative is likely to be produced and the purity is lowered, and it is difficult to remove the sulfuric acid after the reaction. On the other hand, if it is low, the reaction temperature cannot be raised sufficiently and the reaction rate decreases, resulting in poor productivity.

【0036】本工程において、前工程(ハ)で得られた
生成物の硫酸水溶液に対する濃度は、5〜50重量%の
範囲の濃度で行うことが好ましい。濃度が高い場合に
は、反応の制御が困難になり、低い場合には生産性が悪
くなってしまい好ましくない。
In this step, the concentration of the product obtained in the previous step (c) in the aqueous sulfuric acid solution is preferably in the range of 5 to 50% by weight. When the concentration is high, it becomes difficult to control the reaction, and when the concentration is low, productivity is deteriorated, which is not preferable.

【0037】また、本工程における反応温度は、120
〜180℃の範囲で行うことが好ましく、特に140〜
170℃の範囲で行うことが好ましい。反応温度が高い
場合には、反応の制御が困難になり、低い場合には反応
速度が低下し生産性が悪くなってしい好ましくない。
The reaction temperature in this step is 120.
It is preferable to carry out in the range of ~ 180 ° C, especially 140 ~
It is preferably carried out in the range of 170 ° C. When the reaction temperature is high, it becomes difficult to control the reaction, and when the reaction temperature is low, the reaction rate decreases and the productivity deteriorates, which is not preferable.

【0038】本工程における反応時間は、反応温度など
によるが通常1〜24時間で行うことができる。
The reaction time in this step depends on the reaction temperature and the like, but can usually be 1 to 24 hours.

【0039】反応終了後、目的物のフタル酸誘導体の目
標とする純度により、所定回数、上述の(ロ)〜(ニ)
の工程を繰り返し、最終工程の(ホ)の工程を行う。
After completion of the reaction, depending on the target purity of the target phthalic acid derivative, the above-mentioned (b) to (d) are repeated a predetermined number of times.
The above step is repeated, and the final step (e) is performed.

【0040】(4) 工程(ホ)について この工程は、工程(ニ)で得られた生成物を反応液(酸
性水媒体)中から分離する工程である。
(4) Step (e) This step is a step of separating the product obtained in step (d) from the reaction solution (acidic aqueous medium).

【0041】本工程では、その方法として、工程(ニ)
の反応液に直接水と2層状態になる有機溶媒を加え溶解
させ、その後有機層を分液し蒸発乾固する方法がある。
加える有機溶媒としては、水と2層状態になり、生成物
と反応しないものであれば特に限定されるものではない
が、脂肪酸エステル類、ケトン類、エーテル類、ベンゾ
ニトリル類が好ましく、特に脂肪酸エステル類、ケトン
類が好ましい。例えば、酢酸エチル、酢酸イソプロピ
ル、メチルイソブチルケトンなどが挙げられる。使用す
る有機溶媒の量は、生成物を溶解し得る量以上であれば
問題ない。その後、有機層を分液し、必要であれば有機
層を水洗してもよい。その後、蒸発乾固し生成物を得
る。
In this step, the method is as follows:
There is a method in which water and an organic solvent having a two-layered state are directly added to the reaction solution to dissolve it, and then the organic layer is separated and evaporated to dryness.
The organic solvent to be added is not particularly limited as long as it is in a two-layer state with water and does not react with the product, but fatty acid esters, ketones, ethers and benzonitriles are preferable, and fatty acid is particularly preferable. Esters and ketones are preferable. Examples thereof include ethyl acetate, isopropyl acetate, methyl isobutyl ketone and the like. There is no problem with the amount of the organic solvent used as long as it can dissolve the product. After that, the organic layer may be separated, and if necessary, the organic layer may be washed with water. Then, it is evaporated to dryness to obtain the product.

【0042】本工程では、また別の方法として、工程
(ニ)の反応溶液を一旦瀘過し得られた瀘物に有機溶媒
を含有する媒体を加え溶解させ、その後加えた有機溶媒
層が水層と2層状態になるものであれば分液し、有機層
を蒸発乾固し、生成物を得、加えた有機溶媒が水と2層
状態にならないものであれば水を固体が析出するまで加
えその後瀘過、乾燥して生成物を得ることができる。水
と2層状態になる有機溶媒を用いる場合、加える有機溶
媒としては、生成物と反応しないものであれば特に制限
されるものではないが、脂肪酸エステル類、ケトン類、
エーテル類、ベンゾニトリル類が好ましく、特に脂肪酸
エステル類、ケトン類が好ましい。例えば、酢酸エチ
ル、酢酸イソプロピル、メチルイソブチルケトンなどが
挙げられる。使用する有機溶媒の量は、生成物を溶解し
得る量以上であれば問題ない。その後、有機層を分液
し、必要であれば有機層を水洗してもよい。その後、蒸
発乾固し生成物を得る。水と2層状態にならないものを
用いる場合、加える有機溶媒としては、生成物と反応し
ないものであれば特に制限されるものではないが、ケト
ン類、アセトニトリル類、アルコール類が好ましく、特
にケトン類が好ましい。例えば、アセトン、アセトニト
リル、メタノール、エタノールなどが挙げられる。使用
する有機溶媒の量は、生成物を溶解し得る量以上であれ
ば問題ない。その後、水を固体が析出するまで加え、瀘
過、乾燥により生成物を得る。水の量は、固体が析出す
る量以上加えれば問題ないが、例えば、溶媒がアセトン
の場合、重量で5倍以上の水を用いれば良い。
In this step, as another method, the reaction solution of step (d) is once filtered, and a solvent containing an organic solvent is added to the filtered solution to dissolve the filtered solution. If it is in a two-layer state with a layer, liquid separation is performed, the organic layer is evaporated to dryness to obtain a product, and if the added organic solvent is not in a two-layer state with water, a solid of water is precipitated. Then, the product can be obtained by filtration and drying. When an organic solvent that forms a two-layer state with water is used, the organic solvent to be added is not particularly limited as long as it does not react with the product, but fatty acid esters, ketones,
Ethers and benzonitriles are preferable, and fatty acid esters and ketones are particularly preferable. Examples thereof include ethyl acetate, isopropyl acetate, methyl isobutyl ketone and the like. There is no problem with the amount of the organic solvent used as long as it can dissolve the product. After that, the organic layer may be separated, and if necessary, the organic layer may be washed with water. Then, it is evaporated to dryness to obtain the product. When a solvent that does not form a two-layer state with water is used, the organic solvent to be added is not particularly limited as long as it does not react with the product, but ketones, acetonitriles, alcohols are preferable, and ketones are particularly preferable. Is preferred. For example, acetone, acetonitrile, methanol, ethanol and the like can be mentioned. There is no problem with the amount of the organic solvent used as long as it can dissolve the product. Then, water is added until a solid precipitates, and the product is obtained by filtration and drying. There is no problem if the amount of water is added in an amount not less than the amount by which solids are precipitated. For example, when the solvent is acetone, water by weight of 5 times or more may be used.

【0043】以上の工程を行うことで、高純度のフタル
酸誘導体を高収率で得ることが可能となった。
By performing the above steps, it becomes possible to obtain a high-purity phthalic acid derivative in a high yield.

【0044】[0044]

【実施例】以下、本発明を実施例によりさらに具体的に
説明する。
EXAMPLES Hereinafter, the present invention will be described more specifically with reference to examples.

【0045】実施例1 (1)撹拌装置、冷却還流管および温度計を備えた20
0ml三ッ口フラスコに1,4−ビス(3,4−ジシア
ノトリフルオロフェノキシ)テトラフルオロベンゼン1
0gおよび70重量%硫酸水溶液90gを加え、還流温
度で6時間反応を行った。反応終了後、室温まで冷却し
水200mlを加え瀘過し、さらに瀘物を水10mlで
2回洗浄した。瀘物を100mlビーカーに取り出し、
アセトン8mlを加え溶解させた。水80mlを加え固
体を析出させ、析出した固体を瀘過、乾燥し生成物1
0.8gを得た。液体クロマトグラフィーにより分析を
行ったところ1,4−ビス(3,4−ジカルボキシトリ
フルオロフェノキシ)テトラフルオロベンゼンを91.
8%含有することが分かった。
Example 1 (1) 20 equipped with a stirrer, a cooling reflux tube and a thermometer
1,4-bis (3,4-dicyanotrifluorophenoxy) tetrafluorobenzene 1 in a 0 ml three-necked flask.
0 g and 90 g of a 70 wt% sulfuric acid aqueous solution were added, and the reaction was carried out at the reflux temperature for 6 hours. After completion of the reaction, the mixture was cooled to room temperature, 200 ml of water was added and filtered, and the filtrate was washed twice with 10 ml of water. Remove the soot into a 100 ml beaker,
8 ml of acetone was added and dissolved. 80 ml of water was added to precipitate a solid, and the precipitated solid was filtered and dried to obtain a product 1
0.8 g was obtained. Analysis by liquid chromatography revealed that 1,4-bis (3,4-dicarboxytrifluorophenoxy) tetrafluorobenzene was 91.
It was found to contain 8%.

【0046】(2)撹拌装置、冷却還流管および温度計
を備えた200ml三ッ口フラスコに上記生成物(1,
4−ビス(3,4−ジカルボキシトリフルオロフェノキ
シ)テトラフルオロベンゼン91.8%含有)10.8
gおよび70重量%硫酸水溶液90gを加え、還流温度
で6時間反応を行った。反応終了後、室温まで冷却し水
200mlを加え瀘過し、さらに瀘物を水10mlで2
回洗浄した。瀘物を100mlビーカーに取り出し、ア
セトン8mlを加え溶解させた。水80mlを加え固体
を析出させ、析出した固体を瀘過、乾燥し生成物10.
3gを得た。液体クロマトグラフィーにより分析を行っ
たところ1,4−ビス(3,4−ジカルボキシトリフル
オロフェノキシ)テトラフルオロベンゼンを96.4%
含有することが分かった。
(2) In a 200 ml three-necked flask equipped with a stirrer, a cooling reflux tube and a thermometer, the above product (1,
4-bis (3,4-dicarboxytrifluorophenoxy) tetrafluorobenzene 91.8% content) 10.8
g and 90 g of a 70 wt% sulfuric acid aqueous solution were added, and the reaction was carried out at the reflux temperature for 6 hours. After the reaction was completed, the mixture was cooled to room temperature, 200 ml of water was added, and the mixture was filtered.
Washed twice. The filtrate was taken out in a 100 ml beaker, and 8 ml of acetone was added and dissolved. 80 ml of water was added to precipitate a solid, and the precipitated solid was filtered and dried to obtain the product 10.
3 g were obtained. When analyzed by liquid chromatography, 96.4% of 1,4-bis (3,4-dicarboxytrifluorophenoxy) tetrafluorobenzene was obtained.
It was found to contain.

【0047】(3)撹拌装置、冷却還流管および温度計
を備えた200ml三ッ口フラスコに上記生成物(1,
4−ビス(3,4−ジカルボキシトリフルオロフェノキ
シ)テトラフルオロベンゼン96.4%含有)10.3
gおよび70重量%硫酸水溶液90gを加え、還流温度
で6時間反応を行った。反応終了後、室温まで冷却し水
200mlを加え瀘過し、さらに瀘物を水10mlで2
回洗浄した。瀘物を100mlビーカーに取り出し、ア
セトン8mlを加え溶解させた。水80mlを加え固体
を析出させ、析出した固体を瀘過、乾燥し生成物9.8
gを得た。液体クロマトグラフィーにより分析を行った
ところ1,4−ビス(3,4−ジカルボキシトリフルオ
ロフェノキシ)テトラフルオロベンゼンを99.2%含
有することが分かった。
(3) In a 200 ml three-necked flask equipped with a stirrer, a cooling reflux tube and a thermometer, the above product (1,
4-bis (3,4-dicarboxytrifluorophenoxy) tetrafluorobenzene 96.4% content) 10.3
g and 90 g of a 70 wt% sulfuric acid aqueous solution were added, and the reaction was carried out at the reflux temperature for 6 hours. After the reaction was completed, the mixture was cooled to room temperature, 200 ml of water was added, and the mixture was filtered.
Washed twice. The filtrate was taken out in a 100 ml beaker, and 8 ml of acetone was added and dissolved. 80 ml of water was added to precipitate a solid, and the precipitated solid was filtered and dried to obtain a product 9.8.
g was obtained. Analysis by liquid chromatography revealed that it contained 99.2% of 1,4-bis (3,4-dicarboxytrifluorophenoxy) tetrafluorobenzene.

【0048】実施例2 70重量%硫酸水溶液90gの代わりに50%硫酸水溶
液90gを用いた以外は実施例1と同様の方法で反応を
行い、1,4−ビス(3,4−ジカルボキシトリフルオ
ロフェノキシ)テトラフルオロベンゼン9.6gを得
た。液体クロマトグラフィーにより分析を行ったところ
純度は99.1%であった。
Example 2 The reaction was carried out in the same manner as in Example 1 except that 90 g of a 50% sulfuric acid aqueous solution was used instead of 90 g of a 70 wt% sulfuric acid aqueous solution, and 1,4-bis (3,4-dicarboxytricarboxylic acid) was used. 9.6 g of fluorophenoxy) tetrafluorobenzene was obtained. When analyzed by liquid chromatography, the purity was 99.1%.

【0049】実施例3 70重量%硫酸水溶液90gの代わりに80%硫酸水溶
液90gを用いた以外は実施例1と同様の方法で反応を
行い、1,4−ビス(3,4−ジカルボキシトリフルオ
ロフェノキシ)テトラフルオロベンゼン9.8gを得
た。液体クロマトグラフィーにより分析を行ったところ
純度は99.0%であった。
Example 3 The reaction was carried out in the same manner as in Example 1 except that 90 g of 80% sulfuric acid aqueous solution was used instead of 90 g of 70% by weight sulfuric acid aqueous solution, and 1,4-bis (3,4-dicarboxytricarboxylic acid) was used. 9.8 g of fluorophenoxy) tetrafluorobenzene was obtained. When analyzed by liquid chromatography, the purity was 99.0%.

【0050】実施例4 (1)撹拌装置、冷却還流管および温度計を備えた20
0ml三ッ口フラスコに70重量%硫酸水溶液90gを
加え、還流温度まで加熱する。そこへ1,4−ビス
(3,4−ジシアノトリフルオロフェノキシ)テトラフ
ルオロベンゼン10gを1時間かけて投入し、その後、
還流温度で5時間反応を行った。反応終了後、室温まで
冷却し水200mlを加え瀘過し、さらに瀘物を水10
mlで2回洗浄した。瀘物を100mlビーカーに取り
出し、アセトン8mlを加え溶解させた。水80mlを
加え固体を析出させ、析出した固体を瀘過、乾燥し生成
物10.7gを得た。液体クロマトグラフィーにより分
析を行ったところ1,4−ビス(3,4−ジカルボキシ
トリフルオロフェノキシ)テトラフルオロベンゼンを9
2.1%含有することが分かった。
Example 4 (1) 20 equipped with a stirrer, a cooling reflux tube and a thermometer
90 g of 70 wt% sulfuric acid aqueous solution is added to a 0 ml three-necked flask and heated to reflux temperature. 10 g of 1,4-bis (3,4-dicyanotrifluorophenoxy) tetrafluorobenzene was added thereto over 1 hour, and then,
The reaction was carried out at the reflux temperature for 5 hours. After completion of the reaction, the mixture was cooled to room temperature, 200 ml of water was added, and the mixture was filtered.
Washed twice with ml. The filtrate was taken out in a 100 ml beaker, and 8 ml of acetone was added and dissolved. 80 ml of water was added to precipitate a solid, and the precipitated solid was filtered and dried to obtain 10.7 g of a product. Analysis by liquid chromatography revealed that 1,4-bis (3,4-dicarboxytrifluorophenoxy) tetrafluorobenzene was found to be 9
It was found to contain 2.1%.

【0051】(2)撹拌装置、冷却還流管および温度計
を備えた200ml三ッ口フラスコに上記生成物(1,
4−ビス(3,4−ジカルボキシトリフルオロフェノキ
シ)テトラフルオロベンゼン92.1%含有)10.7
gおよび70重量%硫酸水溶液90gを加え、還流温度
で6時間反応を行った。反応終了後、室温まで冷却し水
200mlを加え瀘過し、さらに瀘物を水10mlで2
回洗浄した。瀘物を100mlビーカーに取り出し、ア
セトン8mlを加え溶解させた。水80mlを加え固体
を析出させ、析出した固体を瀘過、乾燥し生成物10.
4gを得た。液体クロマトグラフィーにより分析を行っ
たところ1,4−ビス(3,4−ジカルボキシトリフル
オロフェノキシ)テトラフルオロベンゼンを96.2%
含有することが分かった。
(2) A 200 ml three-necked flask equipped with a stirrer, a cooling reflux tube and a thermometer was charged with the above product (1,
4-bis (3,4-dicarboxytrifluorophenoxy) tetrafluorobenzene 92.1% content) 10.7
g and 90 g of a 70 wt% sulfuric acid aqueous solution were added, and the reaction was carried out at the reflux temperature for 6 hours. After the reaction was completed, the mixture was cooled to room temperature, 200 ml of water was added, and the mixture was filtered.
Washed twice. The filtrate was taken out in a 100 ml beaker, and 8 ml of acetone was added and dissolved. 80 ml of water was added to precipitate a solid, and the precipitated solid was filtered and dried to obtain the product 10.
4 g were obtained. When analyzed by liquid chromatography, 96.2% of 1,4-bis (3,4-dicarboxytrifluorophenoxy) tetrafluorobenzene was obtained.
It was found to contain.

【0052】(3)撹拌装置、冷却還流管および温度計
を備えた200ml三ッ口フラスコに上記生成物(1,
4−ビス(3,4−ジカルボキシトリフルオロフェノキ
シ)テトラフルオロベンゼン96.2%含有)10.4
gおよび70重量%硫酸水溶液90gを加え、還流温度
で6時間反応を行った。反応終了後、室温まで冷却し水
200mlを加え瀘過し、さらに瀘物を水10mlで2
回洗浄した。瀘物を100mlビーカーに取り出し、ア
セトン8mlを加え溶解させた。水80mlを加え固体
を析出させ、析出した固体を瀘過、乾燥し生成物9.4
gを得た。液体クロマトグラフィーにより分析を行った
ところ1,4−ビス(3,4−ジカルボキシトリフルオ
ロフェノキシ)テトラフルオロベンゼンを99.1%含
有することが分かった。
(3) In a 200 ml three-necked flask equipped with a stirrer, a cooling reflux tube and a thermometer, the above product (1,
4-bis (3,4-dicarboxytrifluorophenoxy) tetrafluorobenzene 96.2% content) 10.4
g and 90 g of a 70 wt% sulfuric acid aqueous solution were added, and the reaction was carried out at the reflux temperature for 6 hours. After the reaction was completed, the mixture was cooled to room temperature, 200 ml of water was added, and the mixture was filtered.
Washed twice. The filtrate was taken out in a 100 ml beaker, and 8 ml of acetone was added and dissolved. 80 ml of water was added to precipitate a solid, and the precipitated solid was filtered and dried to obtain a product 9.4.
g was obtained. Analysis by liquid chromatography revealed that it contained 99.1% of 1,4-bis (3,4-dicarboxytrifluorophenoxy) tetrafluorobenzene.

【0053】実施例5 (1)撹拌装置、冷却還流管および温度計を備えた20
0ml三ッ口フラスコに1,4−ビス(3,4−ジシア
ノトリフルオロフェノキシ)テトラフルオロベンゼン1
0gおよび70重量%硫酸水溶液90gを加え、還流温
度で6時間反応を行った。反応終了後、室温まで冷却し
水100mlを加え、さらにメチルイソブチルケトン2
00ml加え析出している固体を溶解させる。有機層を
分液し、水20mlで2回洗浄した。有機層を蒸発乾固
し生成物10.9gを得た。液体クロマトグラフィーに
より分析を行ったところ1,4−ビス(3,4−ジカル
ボキシトリフルオロフェノキシ)テトラフルオロベンゼ
ンを91.5%含有することが分かった。
Example 5 (1) 20 equipped with a stirrer, a cooling reflux tube and a thermometer
1,4-bis (3,4-dicyanotrifluorophenoxy) tetrafluorobenzene 1 in a 0 ml three-necked flask.
0 g and 90 g of a 70 wt% sulfuric acid aqueous solution were added, and the reaction was carried out at the reflux temperature for 6 hours. After completion of the reaction, the mixture was cooled to room temperature, 100 ml of water was added, and methyl isobutyl ketone 2 was added.
Add 00 ml to dissolve the precipitated solid. The organic layer was separated and washed twice with 20 ml of water. The organic layer was evaporated to dryness to obtain 10.9 g of product. Analysis by liquid chromatography revealed that it contained 91.5% of 1,4-bis (3,4-dicarboxytrifluorophenoxy) tetrafluorobenzene.

【0054】(2)撹拌装置、冷却還流管および温度計
を備えた200ml三ッ口フラスコに上記生成物(1,
4−ビス(3,4−ジカルボキシトリフルオロフェノキ
シ)テトラフルオロベンゼン91.5%含有)10.9
gおよび70重量%硫酸水溶液90gを加え、還流温度
で6時間反応を行った。反応終了後、室温まで冷却し水
100mlを加え、さらにメチルイソブチルケトン20
0ml加え析出している固体を溶解させる。有機層を分
液し、水20mlで2回洗浄した。有機層を蒸発乾固し
生成物10.6gを得た。液体クロマトグラフィーによ
り分析を行ったところ1,4−ビス(3,4−ジカルボ
キシトリフルオロフェノキシ)テトラフルオロベンゼン
を95.9%含有することが分かった。
(2) A 200 ml three-necked flask equipped with a stirrer, a cooling reflux tube and a thermometer was charged with the above product (1,
4-bis (3,4-dicarboxytrifluorophenoxy) tetrafluorobenzene 91.5% content) 10.9
g and 90 g of a 70 wt% sulfuric acid aqueous solution were added, and the reaction was carried out at the reflux temperature for 6 hours. After completion of the reaction, the mixture was cooled to room temperature, 100 ml of water was added, and further methyl isobutyl ketone 20
Add 0 ml to dissolve the precipitated solid. The organic layer was separated and washed twice with 20 ml of water. The organic layer was evaporated to dryness to obtain 10.6 g of product. Analysis by liquid chromatography revealed that it contained 95.9% of 1,4-bis (3,4-dicarboxytrifluorophenoxy) tetrafluorobenzene.

【0055】(3)撹拌装置、冷却還流管および温度計
を備えた200ml三ッ口フラスコに上記生成物(1,
4−ビス(3,4−ジカルボキシトリフルオロフェノキ
シ)テトラフルオロベンゼン95.9%含有)10.6
gおよび70重量%硫酸水溶液90gを加え、還流温度
で6時間反応を行った。反応終了後、室温まで冷却し水
100mlを加え、さらにメチルイソブチルケトン20
0ml加え析出している固体を溶解させる。有機層を分
液し、水20mlで2回洗浄した。有機層を蒸発乾固し
生成物10.2gを得た。液体クロマトグラフィーによ
り分析を行ったところ1,4−ビス(3,4−ジカルボ
キシトリフルオロフェノキシ)テトラフルオロベンゼン
を99.0%含有することが分かった。
(3) In a 200 ml three-necked flask equipped with a stirrer, a cooling reflux tube and a thermometer, the above product (1,
4-bis (3,4-dicarboxytrifluorophenoxy) tetrafluorobenzene 95.9% content) 10.6
g and 90 g of a 70 wt% sulfuric acid aqueous solution were added, and the reaction was carried out at the reflux temperature for 6 hours. After completion of the reaction, the mixture was cooled to room temperature, 100 ml of water was added, and further methyl isobutyl ketone 20
Add 0 ml to dissolve the precipitated solid. The organic layer was separated and washed twice with 20 ml of water. The organic layer was evaporated to dryness to give 10.2 g of product. Analysis by liquid chromatography revealed that it contained 99.0% of 1,4-bis (3,4-dicarboxytrifluorophenoxy) tetrafluorobenzene.

【0056】比較例1 撹拌装置、冷却還流管および温度計を備えた200ml
三ッ口フラスコに1,4−ビス(3,4−ジシアノトリ
フルオロフェノキシ)テトラフルオロベンゼン10gお
よび70重量%硫酸水溶液90gを加え、還流温度で6
時間反応を行った。反応終了後、室温まで冷却し水20
0mlを加えた後、析出している生成物を瀘過し、さら
に水10mlで2回洗浄を行った。その後、瀘物を乾燥
することで1,4−ビス(3,4−ジカルボキシトリフ
ルオロフェノキシ)テトラフルオロベンゼンを10.6
g得た。得られた化合物の純度は、液体クロマトグラフ
ィーによる分析の結果91.8%であった。
Comparative Example 1 200 ml equipped with a stirrer, a cooling reflux tube and a thermometer
To a three-necked flask, 10 g of 1,4-bis (3,4-dicyanotrifluorophenoxy) tetrafluorobenzene and 90 g of a 70 wt% sulfuric acid aqueous solution were added, and the mixture was refluxed at a temperature of 6
A time reaction was performed. After the reaction is complete, cool to room temperature and add water 20
After adding 0 ml, the precipitated product was filtered and further washed with 10 ml of water twice. Then, 1,4-bis (3,4-dicarboxytrifluorophenoxy) tetrafluorobenzene was dried at 10.6 by drying the filtrate.
g was obtained. The purity of the obtained compound was 91.8% as a result of analysis by liquid chromatography.

【0057】参考例1 撹拌装置、冷却還流管および温度計を備えた200ml
三ッ口フラスコに1,4−ビス(3,4−ジシアノトリ
フルオロフェノキシ)テトラフルオロベンゼン10gお
よび60重量%硫酸水溶液18.5mlを加え、150
℃で15時間反応を行った。反応終了後、室温まで冷却
し、析出している生成物を瀘過し、さらに水洗浄を行っ
た。その後、瀘物を乾燥することで1,4−ビス(3,
4−ジカルボキシトリフルオロフェノキシ)テトラフル
オロベンゼンを10.3g得た。得られた化合物の純度
は、液体クロマトグラフィーによる分析の結果91.8
%であった。
Reference Example 1 200 ml equipped with a stirrer, a cooling reflux tube and a thermometer
To a three-necked flask, 10 g of 1,4-bis (3,4-dicyanotrifluorophenoxy) tetrafluorobenzene and 18.5 ml of a 60% by weight sulfuric acid aqueous solution were added, and 150
The reaction was carried out at 150C for 15 hours. After completion of the reaction, the reaction mixture was cooled to room temperature, the precipitated product was filtered, and further washed with water. After that, the 1,4-bis (3,3
10.3 g of 4-dicarboxytrifluorophenoxy) tetrafluorobenzene was obtained. The purity of the obtained compound was 91.8 as a result of analysis by liquid chromatography.
%Met.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 (イ)下記一般式(I)で表わされる化
合物を酸性水媒体中で加熱し、下記一般式(II)で表わ
される化合物を含有する生成物を得、(ロ)次いで、得
られた生成物を有機溶媒を含有する媒体中に一旦溶解
し、(ハ)媒体中より生成物を分離し、(ニ)さらに、
得られた生成物を酸性水媒体中で加熱し、(ホ)その
後、得られた酸性水媒体中から生成物を分離する、とす
る工程において、上記(イ)〜(ニ)の工程を行った
後、(ロ)〜(ニ)の工程を少なくとも1回以上繰り返
し行い、最後に(ホ)の工程を行って下記一般式(II)
で表わされるフタル酸誘導体を含有する生成物を得るこ
とを特徴とする製造方法。 【化1】 【化2】
(A) A compound represented by the following general formula (I) is heated in an acidic aqueous medium to obtain a product containing the compound represented by the following general formula (II), and (b) then, The obtained product is once dissolved in a medium containing an organic solvent, (c) the product is separated from the medium, and (d) further,
In the step of heating the obtained product in an acidic aqueous medium and (e) then separating the product from the obtained acidic aqueous medium, the steps (a) to (d) above are performed. After that, the steps (b) to (d) are repeated at least once or more, and finally the step (e) is performed to give the following general formula (II).
A process for producing a product containing a phthalic acid derivative represented by: Embedded image Embedded image
【請求項2】 前記一般式(I)の化合物が、1,4−
ビス(3,4−ジシアノトリフルオロフェノキシ)テト
ラフルオロベンゼンであり、前記一般式(II)の化合物
が、1,4−ビス(3,4−ジカルボキシトリフルオロ
フェノキシ)テトラフルオロベンゼンである請求項1に
記載の製造方法。
2. The compound of general formula (I) is 1,4-
Bis (3,4-dicyanotrifluorophenoxy) tetrafluorobenzene, wherein the compound of the general formula (II) is 1,4-bis (3,4-dicarboxytrifluorophenoxy) tetrafluorobenzene. 1. The manufacturing method according to 1.
【請求項3】 前記(ロ)の工程の有機溶媒を含有する
媒体が、少なくとも50%重量以上のケトン類を含有す
ることを特徴とする請求項1または2に記載の製造方
法。
3. The production method according to claim 1, wherein the medium containing the organic solvent in the step (b) contains at least 50% by weight or more of ketones.
JP26600795A 1995-10-13 1995-10-13 Method for producing phthalic acid derivative Expired - Fee Related JP3739119B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26600795A JP3739119B2 (en) 1995-10-13 1995-10-13 Method for producing phthalic acid derivative

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26600795A JP3739119B2 (en) 1995-10-13 1995-10-13 Method for producing phthalic acid derivative

Publications (2)

Publication Number Publication Date
JPH09110785A true JPH09110785A (en) 1997-04-28
JP3739119B2 JP3739119B2 (en) 2006-01-25

Family

ID=17425081

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP3739119B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6916959B2 (en) 2001-05-11 2005-07-12 Nippon Shokubai Co., Ltd. Halogen-containing aromatic compound

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6916959B2 (en) 2001-05-11 2005-07-12 Nippon Shokubai Co., Ltd. Halogen-containing aromatic compound
US7217827B2 (en) 2001-05-11 2007-05-15 Nippon Shokubai Co., Ltd. Halogen-containing aromatic compound

Also Published As

Publication number Publication date
JP3739119B2 (en) 2006-01-25

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