JPH0368623A - Production of anthracene polyester - Google Patents

Production of anthracene polyester

Info

Publication number
JPH0368623A
JPH0368623A JP20609289A JP20609289A JPH0368623A JP H0368623 A JPH0368623 A JP H0368623A JP 20609289 A JP20609289 A JP 20609289A JP 20609289 A JP20609289 A JP 20609289A JP H0368623 A JPH0368623 A JP H0368623A
Authority
JP
Japan
Prior art keywords
anthracene
polyester
polymer
intrinsic viscosity
anthraquinone
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
JP20609289A
Other languages
Japanese (ja)
Inventor
Yoichi Nakamura
洋一 中村
Noboru Kosho
古庄 昇
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.)
Fuji Electric Co Ltd
Original Assignee
Fuji Electric 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 Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP20609289A priority Critical patent/JPH0368623A/en
Publication of JPH0368623A publication Critical patent/JPH0368623A/en
Pending legal-status Critical Current

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  • Polyesters Or Polycarbonates (AREA)

Abstract

PURPOSE:To obtain stably a highly viscous anthracene polyester by reacting an anthraquinone compound with a reducing agent at a specified temperature or below. CONSTITUTION:An anthracene polyester is obtained by reacting an anthraquinone compound with a reducing agent at a temperature <=50 deg.C. According to this production process a highly viscous anthracene polyester can be stably obtained. Therefore a nonsagging coating fluid can be stably obtained when it is applied to e.g. an electrophotographic photoreceptor.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は、アントラキノン化合物を原料としてアント
ラセン系ポリエステルを製造する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for producing anthracene polyester using an anthraquinone compound as a raw material.

〔従来の技術〕[Conventional technology]

アントラセン系ポリエステルを製造する際に、アントラ
キノン化合物を還元剤1例えば亜ニチオン酸ナトリウム
およびジカルボン酸シバライド。
When producing anthracene polyesters, anthraquinone compounds are treated with reducing agents such as sodium dithionite and dicarboxylic acid civalide.

例えばアゼライン酸ジクロライドと反応させてアントラ
セン系ポリエステルが得られることは従来公知である(
特公昭60−3408号公報参照)〔発明が解決しよう
とする課題〕 しかしながら、従来の製造方法では、何らかの粘度のア
ントラセン系ポリエステルを得ることはできるが、高い
粘度のアントラセン系ポリエステルを安定して得ること
ができないという問題があった。例えば、このアントラ
セン系ポリエステルを電子写真用感光体に適用しようと
すると、液だれを起こさない塗布液を作製するためには
固有粘度にして1.0程度以上を必要とするが、従来の
製造方法では、このような高い粘度のアントラセン系ポ
リエステルを安定して得ることができなかった。
For example, it is known that anthracene polyester can be obtained by reacting with azelaic acid dichloride (
(Refer to Japanese Patent Publication No. 60-3408) [Problems to be Solved by the Invention] However, although it is possible to obtain anthracene polyester with a certain viscosity with the conventional production method, it is difficult to stably obtain anthracene polyester with a high viscosity. The problem was that I couldn't do it. For example, if this anthracene-based polyester is applied to an electrophotographic photoreceptor, an intrinsic viscosity of about 1.0 or higher is required in order to create a coating solution that does not cause dripping, but conventional manufacturing methods However, it has not been possible to stably obtain such a high viscosity anthracene polyester.

この発明は、上述の点を鑑みてなされたものであって、
1.0程度以上の高粘度のアントラセン系ポリエステル
を安定して得ることができる、アントラセン系ポリエス
テルの新規な製造方法を提供することを課題とする。
This invention was made in view of the above points, and
An object of the present invention is to provide a novel method for producing anthracene polyester that can stably obtain anthracene polyester having a high viscosity of about 1.0 or more.

〔課題を解決するための手段〕[Means to solve the problem]

上記の課題は、この発明によれば、アントラキノン化合
物を50℃以下の温度で還元剤と反応させる製造方法に
より解決される。
According to the present invention, the above problems are solved by a production method in which an anthraquinone compound is reacted with a reducing agent at a temperature of 50° C. or lower.

〔作用〕[Effect]

従来公知の技術では、反応温度の制御については、ジカ
ルボン酸シバライドの水との反応性に着目した点でのみ
定性的な知見があるだけで、これ以外の点では、反応温
度は特に制御する必要がないとされてきた。
In the conventionally known technology, regarding the control of the reaction temperature, there is only qualitative knowledge regarding the reactivity of dicarboxylic acid sybaride with water, and there is no need to particularly control the reaction temperature in other respects. It has been said that there is no such thing.

しかしながら、この発明の発明者らは、アントラキノン
化合物の還元温度に着目して検討したところ、アントラ
キノン化合物の還元温度により、生成するアントラセン
系ポリエステルの固有粘度に著しい差異があることを見
いだした。この還元温度を50℃以下とすることにより
高粘度のアントラセン系ポリエステルを安定して得るこ
とが可能となる。
However, the inventors of the present invention focused on the reduction temperature of the anthraquinone compound and found that there is a significant difference in the intrinsic viscosity of the anthracene polyester produced depending on the reduction temperature of the anthraquinone compound. By setting this reduction temperature to 50° C. or lower, it becomes possible to stably obtain a high viscosity anthracene polyester.

〔実施例〕〔Example〕

この発明の実施例を以下に示すが、この発明はこれらの
実施例に限定されるものではない。
Examples of the present invention are shown below, but the present invention is not limited to these examples.

実施例1 アントラキノン104 g 、  亜ニチオン酸ナトリ
ウム348 g 、水酸化ナトリウム400 g 、お
よびトリオクチルメチルアンモニウムクロライド20g
を51の水に投入し、液温を50℃に保ちながら溶解す
るまで攪拌した。この後反応液を15℃まで冷却し、こ
の反応液に、124gのアゼライン酸ジクロライドを含
む21のテトラクロロエタン溶液を加え、激しく攪拌し
た。15分間撹拌したのち、反応液を静置したところ2
層に分離した。分液して下層の有機層を取り出し、30
1のアセトン中に投入したところ、白色微粒子が析出沈
澱した。この沈澱を濾取し、水とアセトンで繰り返し洗
浄したのち、真空乾燥したところ白色粉末を得た。この
ポリマーの固有粘度を測定したところ1.03 (30
℃テトラクロロエタン中)と極めて高い固有粘度をもつ
ポリマーであることが判った。
Example 1 104 g of anthraquinone, 348 g of sodium dithionite, 400 g of sodium hydroxide, and 20 g of trioctylmethylammonium chloride
was added to water in Step 51, and stirred while maintaining the liquid temperature at 50°C until dissolved. Thereafter, the reaction solution was cooled to 15° C., and a tetrachloroethane solution of 21 containing 124 g of azelaic acid dichloride was added to the reaction solution, followed by vigorous stirring. After stirring for 15 minutes, the reaction solution was allowed to stand still.2
Separated into layers. Separate the layers, take out the lower organic layer, and
When the mixture was poured into acetone (No. 1), white fine particles precipitated and precipitated. This precipitate was collected by filtration, washed repeatedly with water and acetone, and then vacuum dried to obtain a white powder. The intrinsic viscosity of this polymer was measured and was 1.03 (30
It was found to be a polymer with an extremely high intrinsic viscosity (°C in tetrachloroethane).

比較例1 アントラキノンなどの溶解温度を52℃にしたこと以外
は、実施例1と同様にしてポリマーを製造した。このポ
リマーの固有粘度を測定したところ0.85 (30℃
テトラクロロエタン中)と不十分な固有粘度を示した。
Comparative Example 1 A polymer was produced in the same manner as in Example 1, except that the melting temperature of anthraquinone and the like was set to 52°C. The intrinsic viscosity of this polymer was measured to be 0.85 (30℃
(in tetrachloroethane) and exhibited insufficient intrinsic viscosity.

実施例2 アントラキノンの代わりに2,6−ジメトキジアントラ
キノン134gにしたこと以外は、実施例1と同様にし
てポリマーを製造した。このポリマーの固有粘度を測定
したところ1.15 (30℃テトラクロロエタン中〉
 と極めて高い固有粘度をもつポリマーであることが判
った。
Example 2 A polymer was produced in the same manner as in Example 1, except that 134 g of 2,6-dimethoxydianthraquinone was used instead of anthraquinone. The intrinsic viscosity of this polymer was measured to be 1.15 (in tetrachloroethane at 30°C).
The polymer was found to have extremely high intrinsic viscosity.

実施例3 アントラキノンの代わりに2.6−ジェトキシアントラ
キノン148 gにしたこと以外は、実施例1と同様に
してポリマーを製造した。このポリマーの固有粘度を測
定したところ1.21 (30℃テトラクロロエタン中
)と極めて高い固有粘度をもつポリマーであることが判
った。
Example 3 A polymer was produced in the same manner as in Example 1, except that 148 g of 2,6-jethoxyanthraquinone was used instead of anthraquinone. When the intrinsic viscosity of this polymer was measured, it was found that the polymer had an extremely high intrinsic viscosity of 1.21 (in tetrachloroethane at 30° C.).

実施例4 アゼライン酸ジクロライドの代わりにドデカンニ酸ジク
ロライド176gにしたこと以外は、実施例1と同様に
してポリマーを製造した。このポリマーの固有粘度を測
定したところ1.32 (30℃テトラクロ゛ロエタン
中)と極めて高い固有粘度をもつポリマーであることが
判った。
Example 4 A polymer was produced in the same manner as in Example 1, except that 176 g of dodecanoic acid dichloride was used instead of azelaic acid dichloride. When the intrinsic viscosity of this polymer was measured, it was found to be a polymer with an extremely high intrinsic viscosity of 1.32 (in tetrachloroethane at 30° C.).

実施例5 アントラキノンの代わりに2.6−ジメトキジアントラ
キノン134gにし、 アゼライン酸ジクロライドの代
わりにドデカンニ酸ジクロライド176gにしたこと以
外は、実施例1と同様にしてポリマーを製造した。この
ポリマーの固有粘度を測定したところ1.45 (30
℃テトラクロロエタン中)と極めて高い固有粘度をもつ
ポリマーであることが判った。
Example 5 A polymer was produced in the same manner as in Example 1, except that 134 g of 2,6-dimethoxydianthraquinone was used instead of anthraquinone, and 176 g of dodecanoic acid dichloride was used instead of azelaic acid dichloride. The intrinsic viscosity of this polymer was measured to be 1.45 (30
It was found to be a polymer with an extremely high intrinsic viscosity (°C in tetrachloroethane).

〔発明の効果〕〔Effect of the invention〕

Claims (1)

【特許請求の範囲】[Claims] 1)アントラキノン化合物を50℃以下の温度で還元剤
と反応させることを特徴とするアントラセン系ポリエス
テルの製造方法。
1) A method for producing anthracene polyester, which comprises reacting an anthraquinone compound with a reducing agent at a temperature of 50° C. or lower.
JP20609289A 1989-08-09 1989-08-09 Production of anthracene polyester Pending JPH0368623A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20609289A JPH0368623A (en) 1989-08-09 1989-08-09 Production of anthracene polyester

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20609289A JPH0368623A (en) 1989-08-09 1989-08-09 Production of anthracene polyester

Publications (1)

Publication Number Publication Date
JPH0368623A true JPH0368623A (en) 1991-03-25

Family

ID=16517677

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20609289A Pending JPH0368623A (en) 1989-08-09 1989-08-09 Production of anthracene polyester

Country Status (1)

Country Link
JP (1) JPH0368623A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2350617A (en) * 1999-06-02 2000-12-06 Nissan Chemical Ind Ltd Polymers of diaminoanthracene and anthraquinone

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5796010A (en) * 1980-12-09 1982-06-15 Asahi Chem Ind Co Ltd High polymeric compound of anthracene
JPS5798523A (en) * 1980-12-12 1982-06-18 Asahi Chem Ind Co Ltd Production of aromatic polyester
JPS58102947A (en) * 1981-12-15 1983-06-18 Asahi Chem Ind Co Ltd Novel electrophotographic receptor
JPS603408A (en) * 1983-06-20 1985-01-09 Toshiba Corp Controller for geothermal turbine
JPS60179420A (en) * 1984-02-27 1985-09-13 Asahi Chem Ind Co Ltd Anthracene skeleton-containing polycarbonate

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5796010A (en) * 1980-12-09 1982-06-15 Asahi Chem Ind Co Ltd High polymeric compound of anthracene
JPS5798523A (en) * 1980-12-12 1982-06-18 Asahi Chem Ind Co Ltd Production of aromatic polyester
JPS58102947A (en) * 1981-12-15 1983-06-18 Asahi Chem Ind Co Ltd Novel electrophotographic receptor
JPS603408A (en) * 1983-06-20 1985-01-09 Toshiba Corp Controller for geothermal turbine
JPS60179420A (en) * 1984-02-27 1985-09-13 Asahi Chem Ind Co Ltd Anthracene skeleton-containing polycarbonate

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2350617A (en) * 1999-06-02 2000-12-06 Nissan Chemical Ind Ltd Polymers of diaminoanthracene and anthraquinone
GB2364062A (en) * 1999-06-02 2002-01-16 Nissan Chemical Ind Ltd Polymers from diaminoanthracene and anthraquinone
GB2364062B (en) * 1999-06-02 2003-05-14 Nissan Chemical Ind Ltd Polymers from diaminoanthracene and anthraquinone

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