JPS58109479A - Preparation of tetracarboxylic acid anhydride - Google Patents

Preparation of tetracarboxylic acid anhydride

Info

Publication number
JPS58109479A
JPS58109479A JP56206079A JP20607981A JPS58109479A JP S58109479 A JPS58109479 A JP S58109479A JP 56206079 A JP56206079 A JP 56206079A JP 20607981 A JP20607981 A JP 20607981A JP S58109479 A JPS58109479 A JP S58109479A
Authority
JP
Japan
Prior art keywords
anhydride
acid
tca
acid anhydride
tricarboxy
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
JP56206079A
Other languages
Japanese (ja)
Other versions
JPH031313B2 (en
Inventor
Hitoshi Oka
岡 仁志
Yoshinori Yoshida
吉田 淑則
Hideetsu Fujiwara
秀悦 藤原
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.)
JSR Corp
Nippon Synthetic Chemical Industry Co Ltd
Original Assignee
Nippon Synthetic Chemical Industry Co Ltd
Japan Synthetic Rubber 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 Synthetic Chemical Industry Co Ltd, Japan Synthetic Rubber Co Ltd filed Critical Nippon Synthetic Chemical Industry Co Ltd
Priority to JP56206079A priority Critical patent/JPS58109479A/en
Publication of JPS58109479A publication Critical patent/JPS58109479A/en
Publication of JPH031313B2 publication Critical patent/JPH031313B2/ja
Granted legal-status Critical Current

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  • Furan Compounds (AREA)
  • Pyrane Compounds (AREA)
  • Heterocyclic Carbon Compounds Containing A Hetero Ring Having Oxygen Or Sulfur (AREA)

Abstract

PURPOSE:To prepare the titled compound useful as a raw material of a polyamidic acid which is a precursor of polyimide, in high purity and efficiency, by reacting an acid anhydride with 2,3,5-tricarboxy-cyclopentane-acetic acid in an organic solvent. CONSTITUTION:2,3,5-Tricarboxy-cyclopentane-acetic acid anhydride is prepared by reacting an acid anhydride such as acetic anhydride, propionic anhydride, butyric anhydride, etc. with 2,3,5-tricarboxy-cyclopentane-acetic acid of formula in an organic solvent such as benzene, toluene, oxylene, ethyl ether, etc. EFFECT:The compound can be prepared in a short reaction time in high yield.

Description

【発明の詳細な説明】 本発明はテトラカルボン酎無水物、特に2,3゜5−ト
リ力ルボキシーシクロペンタノーア七チックアシッド(
以下「TCAJとトす。)C無水物を製造する方法に関
するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to tetracarboxylic anhydride, particularly 2,3゜5-trihydroxycyclopentanoacid (
Hereinafter referred to as "TCAJ", it relates to a method for producing C anhydride.

一般にテトラカルボン酸け、ポリアミド又はポリイミド
の原料として、またエホキシU脂の硬化剤、、その・他
として有用であり、具体的にはヒロメリット耐等の芳香
族テトラカルボン酸、フタンテトラカルボン酸等の脂肪
族テトラカルホンeがよ(2) 〈知【れている。
It is generally useful as a raw material for tetracarboxylic acid, polyamide or polyimide, and as a curing agent for epoxy U resin, etc. Specifically, aromatic tetracarboxylic acids such as Hiromellitai, phthanetetracarboxylic acids Aliphatic tetracarphones such as (2) are known.

MJtかるテトラカルボン酸の1和IKTcAが慶、り
、これは次の構造式で示される環枦脂肪族テトラカルボ
ン酸である。
The monomer of MJt tetracarboxylic acid, IKTcA, is a cyclic aliphatic tetracarboxylic acid represented by the following structural formula.

2 コ(D TCA tri 、1秦的に安価に得らねるジ
シクロペンタジェンをオゾン分解し、更に:A酪化水素
によシ酸什する方法(英国特許第872.355号明細
書又はジャーナル オプ オーガニックケミストリー(
J。Org、 Chen。)第28巻1o号2537〜
2541 )1(1963年)参照)、又はジシクロペ
ンタジェンを水和して得らtするヒドロキシ−ジシクロ
ペンタジェンを硝酪酸什する方法(ドイツ特許給107
8120号四却1書参照)、その仙の方法によって得る
ことができる。
2. (D TCA tri, 1. A method of ozonolyzing dicyclopentadiene, which cannot be obtained at low cost in Qin, and further adding silicic acid with hydrogen butyride (British Patent No. 872.355 specification or journal Op Organic Chemistry (
J. Org, Chen. ) Volume 28, No. 1o, 2537~
2541) 1 (1963)), or a method of adding nitric butyric acid to hydroxy-dicyclopentadiene obtained by hydrating dicyclopentadiene (German Patent No. 107)
(Refer to No. 8120, Book 1), it can be obtained by that immortal method.

このTCAHlそのttで、ポリアミドヌにポリイミド
の原料とし、て、またエポキシ柚脂(3) の硬什剤等と[て充分に使用し得るものではあるか、成
る和・の用途に供する場合、例えは有機ジアミンとの反
応によりポリイミドの前躯体であるポリアミド酸を製造
する場合には、TCAそのものでなくその加水物を用い
たときの力がより高い重合用のものめ・得られる等の利
点があり、このため、TCAの加水物を高い効率で製造
し得る方法の開発が望まれていた。
Is it possible to use this TCAH as a raw material for polyamide, polyimide, and as a hardening agent for epoxy citrus resin (3)? When producing polyamic acid, which is a precursor of polyimide, by reaction with organic diamine, there are advantages such as the ability to obtain a polymerization agent with higher strength when using TCA's hydrate rather than TCA itself. Therefore, it has been desired to develop a method that can produce a TCA hydrate with high efficiency.

TCAの加水物の製造方法については、ドイツ特許第1
078120号明細書に1蓼がt、シ、そねは、TCA
とアセチルクロライドを室温で指押しながら3〜5週間
の間反応を行ない、その後貞空乾燥し更にアセチルクロ
ライドを小餡加えて濾過し、ベンゼンyrより洗浄する
方法であって融点170〜172℃のものが得られるが
、この方法は非常に長い反応時間を必要とする上収率も
約40%と低く、従って非常に効率が低く、しかも生成
物の純度が低い欠点がある。
Regarding the production method of TCA hydrate, German patent No. 1
078120 specification 1 蓼がt, shi, sonewa, TCA
and acetyl chloride at room temperature for 3 to 5 weeks, followed by drying in air, adding a small amount of acetyl chloride, filtering, and washing with benzene yr. However, this method requires a very long reaction time and has a low yield of about 40%, resulting in very low efficiency and low purity of the product.

本発明者らは、以」〕の如き事情に基き、鋭意研究を重
ねた結果本発明を完敗するr(至ったもので特開昭58
−109479(2) あシ、本発明の目的は、高い反応効率でTCAの無水物
を製造することのできる方法を提供するにある。
The inventors of the present invention have conducted extensive research based on the following circumstances, and as a result have completely failed in the present invention.
-109479(2) An object of the present invention is to provide a method capable of producing TCA anhydride with high reaction efficiency.

本発明について詳細に説明すると、本発明においては、
TCAを酸無水物と有機溶媒中で反応せしめることによ
シ、TCAの加水物をi!ll造する。
To explain the present invention in detail, in the present invention,
By reacting TCA with an acid anhydride in an organic solvent, a hydrate of TCA is made into i! ll build.

本発明において使用する酸無水物は、通常、有機カルボ
ン酸の無水物であり、無水酢酸、炉水プロピオン酸、無
水酪酸、無水コハク酸、無水マレイン酸、無水グルタル
酸、無水フタル酸などを例示することができるが、好ま
しい有機カルボン酸無水物は脂肪族カルボン酸の無水物
、特に無水酢酸、無水プロピオン酸、無水酪e’y;r
どの・脂肪族モノカルボン醗の加水物である。
The acid anhydride used in the present invention is usually an anhydride of an organic carboxylic acid, and examples include acetic anhydride, reactor water propionic acid, butyric anhydride, succinic anhydride, maleic anhydride, glutaric anhydride, and phthalic anhydride. However, preferred organic carboxylic acid anhydrides include anhydrides of aliphatic carboxylic acids, particularly acetic anhydride, propionic anhydride, butyric anhydride;
It is a hydrated product of aliphatic monocarboxylic alcohol.

1だ本発明に好適に使用される有機溶媒とし、ては、そ
れ自体が目標生成物であるTCAの無水物を洛解しない
ものが好1しく、更に、使用きれる酸無水物と相溶性の
大きいものが好ましく、このような有機溶媒を使用する
ことによって高純度のTCAの無水物を容y、に得るこ
とができる。この(5) ような1機溶媒としては、例えば芳香族炭化水素類、多
トン類又はエーテル類があり、具μ的には、ベンゼン、
トルエン、キシレン、エチルベンゼン、イソプロピルベ
ンゼン、メチルエチルナトン、メチルプロピルウトン、
メチルイソブチルケトン、メチルヘキシル+)ン、エチ
ルブチルケトン、ジイソブチルケトン、エチルエーテル
、イソプロピルエーテル、ブチルエーテル、ヘキシルニ
ーチル、その他を挙けることができる。
1. The organic solvent preferably used in the present invention is preferably one that does not degrade the anhydride of TCA, which is the target product, and is also compatible with the acid anhydride to be used. Larger solvents are preferred, and by using such organic solvents, it is possible to obtain a large amount of highly purified anhydride TCA. Examples of monosolvents such as (5) include aromatic hydrocarbons, polytons, and ethers, and specifically, benzene,
Toluene, xylene, ethylbenzene, isopropylbenzene, methylethylnaton, methylpropyluthone,
Examples include methyl isobutyl ketone, methylhexyl+)ton, ethyl butyl ketone, diisobutyl ketone, ethyl ether, isopropyl ether, butyl ether, hexylnityl, and others.

次に反応条件について説明する0使用すべき酸無水物の
シは、当該酪・熱水物によって定量的に脱水作用を行わ
しむるために1通常TCAのモル数の2倍以上を使用す
るが、好ましくけ2〜50倍モル使用する。有機溶媒の
1は、その和1・によっても異なるか、好ましくけ酸無
水物の重量の01〜10倍程度とさねる。1だ、反応温
度は打着[くけ20℃V上であり、実際上は還流しなが
ら反応を行なうようにすれけ、一層高い反応効率が得ら
ねる。反応時間は、反応温度によっても異なるが、還流
温良で反応を実行する場合に1、通常(6) 0.2〜lO時間である。上記反応によって得られるT
CAの無水物は、通常2無水物であるが1無水物も得る
ことができる。
Next, we will explain the reaction conditions. 0. The amount of acid anhydride to be used is usually at least twice the number of moles of TCA in order to quantitatively dehydrate the butyrothermal solution. , preferably used in an amount of 2 to 50 times the mole. The amount of the organic solvent varies depending on the sum of the organic solvents, and is preferably about 0.1 to 10 times the weight of the silicic anhydride. 1, the reaction temperature is above 20°C, and in practice the reaction must be carried out under reflux, making it impossible to obtain higher reaction efficiency. The reaction time varies depending on the reaction temperature, but is 1 hour when the reaction is carried out at a good reflux temperature, and usually (6) 0.2 to 10 hours. T obtained by the above reaction
The anhydride of CA is usually dianhydride, but monoanhydride can also be obtained.

本発明は以上のような方法であるので、後述する実施例
からも明かがように、目的とするTCAの無水物を反応
効率良く、即ち短い反応時間で、しかも高い収率で確実
に製造することができる。
Since the present invention is a method as described above, it is possible to reliably produce the target anhydride of TCA with high reaction efficiency, that is, in a short reaction time, and in high yield, as will be clear from the examples described later. be able to.

次に本発明を実施例によって具体的に説明するが、本発
明けこ1らの実施例に限定されるものではない。
EXAMPLES Next, the present invention will be specifically explained with reference to Examples, but the present invention is not limited to these Examples.

実施例1 容f!!2tのフラスコK ST CA 100 g 
(0,385モル)と無水酢$500g(4,90モル
)及びトルエン750gを仕込み、還流させながら3時
間反応せしめ、その後反応液を温度20℃で48時間放
置して晶析を行ない、析出した結晶を炉別して取シ出し
、トルエンによシ洗浄した後一温度80℃で減圧乾燥を
行なって、融点190℃の白色粉末65gを得た。収率
は75モル%である。
Example 1 Yong f! ! 2t flask KST CA 100g
(0,385 mol), anhydrous vinegar $500 g (4,90 mol), and toluene 750 g were reacted for 3 hours under reflux, and then the reaction solution was left at a temperature of 20°C for 48 hours to perform crystallization. The resulting crystals were taken out in a furnace, washed with toluene, and then dried under reduced pressure at a temperature of 80°C to obtain 65 g of a white powder with a melting point of 190°C. The yield is 75 mol%.

得らまた白色粉末をテトラヒドロフランに溶゛解(7) せしめT液体クロマトグラフィーで調べたところ、目的
物であるTCAの2無水物に相当するピーク以外の、原
料であるTCA ′EtびTCAの1無水物のピークは
トレースであシ、この結果、高純度のTCAの2無水物
かWられていることが確認された。
When the obtained white powder was dissolved in tetrahydrofuran (7) and examined by T liquid chromatography, it was found that other than the peak corresponding to the target TCA dianhydride, the raw material TCA 'Et and TCA 1 were detected. The anhydride peak was traced, and as a result, it was confirmed that high purity TCA dianhydride was being traced.

史に1辻の白色粉末について赤外線吸収スペクトルを測
定した。そのチャートを第1図に示す。
The infrared absorption spectrum of a white powder was measured once in history. The chart is shown in FIG.

このチャートにおいて、177QcIn−1及び182
0clL−”の位齢に酸無水物の−COKよる吸収がト
シめられる一力、カルボン酷′の−COによる 170
0C111−’での吸取屑び一0HKよる3 400c
m″″1刊近での吸収か認められず、これらの分析から
も当該白色粉末ViTCAの2力1〔水物であることが
r4詔された。
In this chart, 177QcIn-1 and 182
The absorption of acid anhydride by -COK is enhanced at the age of 0 clL-, and the absorption of carbon by -CO is 170
0C111-' 3 400c by 0HK
No absorption was observed in the vicinity of m''''1 volume, and these analyzes also confirmed that the white powder ViTCA was a 2-water substance.

実施例2 ゝ 実施例IKおけるトルエンの代りに、メチルイソブ
チルケトンを治彬溶媒として用いたほかは、実施例1と
同様の操作を行ない、W・点188℃の白色粉末47g
を得た。収率け55モル%である。
Example 2 ゝ The same operation as Example 1 was carried out except that methyl isobutyl ketone was used as a treatment solvent instead of toluene in Example IK, and 47 g of white powder with a W point of 188°C was obtained.
I got it. The yield was 55 mol%.

そ【て実施例1におけると同様に液体クロマトグラフィ
ー及び赤外線吸収スペクトルによる分析の結果、当該白
色粉末けTCAの2無水物であることか確認された。
As in Example 1, analysis by liquid chromatography and infrared absorption spectroscopy confirmed that the white powder was TCA dianhydride.

実施例3 実施例1におけるトルエンの代りにイソプロピルエーテ
ル500gを有機溶媒として用いたほかは、実施例1と
同様の操作を行ない、融点189℃の白色粉末53gを
得た。収率は62モル%である。そして実施例1におけ
ると同様に液体クロマトグラフィー及び赤外線吸収スペ
クトルによる分析の結果、当該白色粉末はTCAの2無
水物であることが確認された。
Example 3 The same operation as in Example 1 was performed except that 500 g of isopropyl ether was used as an organic solvent instead of toluene in Example 1, to obtain 53 g of a white powder with a melting point of 189°C. The yield is 62 mol%. As in Example 1, analysis by liquid chromatography and infrared absorption spectroscopy confirmed that the white powder was TCA dianhydride.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は、本発明の一実施例による生成物の赤外線吸秒
スペクトルのチャートである。
FIG. 1 is a chart of an infrared absorption spectrum of a product according to an embodiment of the present invention.

Claims (1)

【特許請求の範囲】[Claims] 1、)2,3.5−)リカルボキシーシクロペンタンー
アセチックアシツドを酸無水物と1ris中で反発せし
めて2,3.5−)リカルボキシーシクロペンタノーア
七チック7シツドの輝水物を得ることを特徴とするテト
ラカルボン酎無水物の製造方法。
1.) 2,3.5-) Licarboxycyclopentane-acetic acid is repelled with acid anhydride in 1ris to produce 2,3.5-) Licarboxycyclopentanol 7-side phosphorescent product. A method for producing tetracarboxylic chuan anhydride, characterized in that it obtains.
JP56206079A 1981-12-22 1981-12-22 Preparation of tetracarboxylic acid anhydride Granted JPS58109479A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56206079A JPS58109479A (en) 1981-12-22 1981-12-22 Preparation of tetracarboxylic acid anhydride

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56206079A JPS58109479A (en) 1981-12-22 1981-12-22 Preparation of tetracarboxylic acid anhydride

Publications (2)

Publication Number Publication Date
JPS58109479A true JPS58109479A (en) 1983-06-29
JPH031313B2 JPH031313B2 (en) 1991-01-10

Family

ID=16517472

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56206079A Granted JPS58109479A (en) 1981-12-22 1981-12-22 Preparation of tetracarboxylic acid anhydride

Country Status (1)

Country Link
JP (1) JPS58109479A (en)

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