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JPH0578575B2 - - Google Patents
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JPH0578575B2 - - Google Patents

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Publication number
JPH0578575B2
JPH0578575B2 JP7867984A JP7867984A JPH0578575B2 JP H0578575 B2 JPH0578575 B2 JP H0578575B2 JP 7867984 A JP7867984 A JP 7867984A JP 7867984 A JP7867984 A JP 7867984A JP H0578575 B2 JPH0578575 B2 JP H0578575B2
Authority
JP
Japan
Prior art keywords
electrode
mol
pyridine
electrolytic
film
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 - Lifetime
Application number
JP7867984A
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Japanese (ja)
Other versions
JPS60223817A (en
Inventor
Kenichi Morita
Noboru Koyama
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.)
Toray Industries Inc
Original Assignee
Toray Industries Inc
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Filing date
Publication date
Application filed by Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP7867984A priority Critical patent/JPS60223817A/en
Publication of JPS60223817A publication Critical patent/JPS60223817A/en
Publication of JPH0578575B2 publication Critical patent/JPH0578575B2/ja
Granted legal-status Critical Current

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    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N27/00Investigating or analysing materials by the use of electric, electrochemical, or magnetic means
    • G01N27/02Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating impedance
    • G01N27/04Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating impedance by investigating resistance
    • G01N27/12Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating impedance by investigating resistance of a solid body in dependence upon absorption of a fluid; of a solid body in dependence upon reaction with a fluid, for detecting components in the fluid
    • G01N27/125Composition of the body, e.g. the composition of its sensitive layer
    • G01N27/126Composition of the body, e.g. the composition of its sensitive layer comprising organic polymers

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Physics & Mathematics (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Biochemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • General Physics & Mathematics (AREA)
  • Immunology (AREA)
  • Pathology (AREA)
  • Polyoxymethylene Polymers And Polymers With Carbon-To-Carbon Bonds (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

〔技術分野〕 本発明は、複素環式化合物の改良された電解酸
化重合方法に関するものである。 〔従来技術とその問題点〕 従来、複素環式化合物などを有機溶媒中で電解
酸化重合することにより、電気伝導性電極基体上
に重合体膜が得られることが知られている。 これらの重合体には種々の電気活性が認めら
れ、電池用の新しい電極の実現、電気化学センサ
ー、エレクトロクロミツクデイスプレーなどの材
料として有望視されている。 しかし、従来の方法によつて得られる重合体膜
は、表面の平滑性や電極基体との密着性などに問
題があり、安定した特性を得ることが難しかつ
た。 〔発明の目的〕 本発明の目的は、表面の平滑性、電極基体との
密着性に優れた複素環式化合物の重合体膜を得る
ための電解酸化重合方法を提供することにある。 〔発明の構成〕 本発明は、ピロール、インドール、カルバゾー
ル、ジベンゾフランおよびジベゾチオフエンから
選ばれた複素環式化合物の有機溶媒中での電解酸
化重合に際し、アミンを添加することを特徴とす
る改良された電解酸化重合方法に関するものであ
る。 本発明では第1図に示すような装置を用いて電
解酸化重合を行なう。これは電解反応を行なう場
合、ごく一般的に用いられる三電極式電解槽と呼
ばれるもので、各室間にあるガラスフイルターは
必ずしも必要としない。この電解槽に電解酸化重
合液を注入し、動作電極と対極との間に所定の電
圧を印加することにより、重合反応が開始され動
作電極上に重合体膜を形成する。膜の厚さ(重合
体の量)は通電した電気量で調節する。両極間に
印加する電圧の大きさは、電解酸化重合液の電圧
−電流特性を測定することにより、最も効率の良
い値を求めることができる。 動作電極および対極には白金、炭素、ネサガラ
ス、ステンレスなどの電気伝導性物質が用いられ
る。この場合、対極の表面積はなるべく大きい方
が高い効率を得ることができる。 基準電極には塩化カリウム飽和カロメル電極、
塩化ナトリウム飽和カロメル電極、銀/塩化銀電
極などの基準電位の得られるものが用いられる
が、用いる電解酸化重合液中の支持電解質の種類
により、電極の内部液と反応を起して析出物を生
ずることがあるので、このような場合には適当な
ものを選択する必要がある。 本発明で用いる電解酸化重合液は、重合単量体
である複素環式化合物と、支持電解質およびアミ
ン添加剤を有機溶媒に溶かして調製される。この
液中に窒素ガスを10〜20分間通気してから反応に
用いる。 支持電解質は、過塩素酸リチウム、過塩素酸ソ
ーダ、硫酸ソーダ、テトラアルキルアンモニウム
テトラフルオロボレイト、トリフルオロ酢酸ナト
リウムなどが挙げられるが、用いる溶媒に可溶で
しかも重合単量体や添加剤と反応を起さないこと
を必要とする。その添加量は通常0.1モル/程
度が用いられる。 本発明で用いることのできる有機溶媒は、重合
単量体、支持電解質およびアミン添加剤をすべて
溶解できるものならば特に制限はない。具体的に
は、アセトニトリル、テトラヒドロフラン、プロ
ピレンカーボネート、ベンゾニトリルなどが挙げ
られる。 本発明で用いるアミン添加剤は、電解酸化重合
しないものであれば特に限定されないが、具体例
としては、メチルアミン、エチルアミン、ジメチ
ルアミン、トリメチルアミン、アリルアミン、シ
クロヘキシルアミン、ピリジン、ピラジン、キノ
リンなどが挙げられる。これら添加剤の量は、重
合単量体1モルに対し、0.1モル〜5.0モルの範囲
が好ましく、5.0モル以上の添加では重合反応の
阻害が認められる。反応溶媒に対する添加剤の量
は、0.01〜10.0モル/の範囲が好ましい。 〔発明の効果〕 本発明を用いて得られる重合体膜は、従来のも
のに比べて均一性、表面の平滑性および電極基板
との密着性に優れており、このことは実用に際
し、安定した性能が得られるなどの効果がある。 以下実施例を挙げて、本発明をさらに具体的に
説明する。 実施例 1〜3 電解酸化重合は第1図に示す装置で行なつた。
動作電極には、1×4cm、厚さ1mm、表面抵抗10
Ωの酸化インジウムネサガラスを用い、電解酸化
重合液との接触面積が2cm2になるように設置し
た。対極には厚さ0.1mm、表面積15cm2の白金板を
用いた。基準電極には塩化ナトリウム飽和カロメ
ル電極を用いた。 電解酸化重合液は、ピロール0.67g(0.1モ
ル/)、過塩素酸ナトリウム2.45g(0.2モル/
)、ピリジン0.79g(0.1モル/)〜3.16g
(0.4モル/)をアセトニトリルに溶解し、全容
を100mlとして調製した。ピリジンの添加量が0.1
モル/のものを実施例1、0.2モル/のもの
を実施例2、0.4モル/のものを実施例3とし
た。この液中に各々窒素ガスを15分間通気した
後、三電極式電解槽に注入した。動作電極に各々
1.1Vの電圧を印加して重合を開始し、通電量が
0.2クーロン/cm2に達した時点で反応を終了した。 動作電極上に形成した重合体膜は、アセトニト
リルで洗浄後、乾燥してから評価に用いた。膜厚
および表面平滑性の測定には薄膜段差計を用い
た。実施例1〜3の測定結果は表1のとおりであ
つた。 ここでRとはピリジン添加率であり、単量体と
ピリジンのモル比を表わす。T1およびT2は、第
2図に示すようにそれぞれ膜厚9および表面突起
10を表わす。従つて表面突起T2の値が小さく
なるほど膜表面の平滑性は増す。 比較例 1 ピリジンを添加しないことと、印加電圧を
0.9Vとしたこと以外は、実施例1と同じ方法で
行なつた。得られた膜の特性は表1のとおりであ
つた。 ピリジン添加率Rと膜厚T1および表面突起T2
との関係を図示すると、それぞれ第3図および第
4図のようになり、比較例1の膜の特性は図上B
点で表わされる。これに対して実施例1〜3で得
た膜の特性は、それぞれP1〜P3点で表わされる。
この結果、ピリジンを添加することにより膜厚が
やや減少する傾向にあるものの膜の表面平滑性が
飛躍的に改善されることがわかる。またピリジン
の添加により、重合体膜の電極基板との接着性が
向上することも認められた。すなわち、重合体膜
の付着した電極を水の中に数分間浸漬した後乾燥
する操作を数回くり返したところ、比較例1で得
られたものは完全に剥離したが、実施例1〜3で
得られたものはいずれも変化しなかつた。 実施例 4 電解酸化重合液は、ジベンゾチオフエン1.86g
(0.1モル/)、過塩素酸ナトリウム2.45g(0.2
モル/)、ピリジン2.37g(0.3モル/)をア
セトニトリルに溶解し、全容を100mlとして調製
した。動作電極に2.2Vの電圧を印加して重合を
開始し、通電量が0.50クーロン/cm2に達した時点
で反応を終了した。その他の操作は実施例1と同
様に行なつた。 得られた重合体膜は、電極基板に均一に付着し
ていた。膜特性の測定結果は表1に記載のとおり
であつた。 比較例 2 ピリジンを添加しないこと以外は、実施例4と
同様に行なつた。重合体はほとんど電極に付着し
なかつた。 実施例 5 単量体にインドール1.17g(0.1モル/)を
用い、印加電圧を2.0Vとした他は実施例4と同
様に実施した。 均一な重合体膜が得られた。膜の特性は表1の
とおりであつた。 比較例 3 ピリジンを添加しなかつたことと、印加電圧を
1.35Vとしたこと以外は実施例5と同様に行なつ
た。 重合体は生成したものの大部分は、電極基板か
ら脱落してしまつた。 実施例 6 電解酸化重合液は、カルバゾール0.84g(0.05
モル/)、テトラブチルアンモニウムヘキサフ
ルオロホスフエイト7.74g(0.2モル/)、ピリ
ジン1.19g(0.15モル/)をアセトニトリルに
溶解し、全容を100mlとして調製した。動作電極
に2.5Vの電圧を印加して重合を開始し、10分後
に反応を終終了した。その他の操作は実施例1と
同様に行なつた。 均一な重合体膜が得られた。膜の特性は表1に
記載したとおりであつた。 比較例 4 ピリジンを添加しないこと以外は実施例6と同
様に行なつた。重合体は電極基板に均一に付着し
なかつた。膜特性は表1のとおりであつた。 実施例 7 単量体にジベンゾフラン0.84g(0.05モル/
)を用い、印加電圧を3.5Vとしたこと以外は
実施例6と同様に行なつた。 均一で光沢のある重合体膜が得られた。膜特性
は表1のとおりであつた。 比較例 5 ピリジンを添加しないこと以外は、実施例7と
同様に行なつた。 重合体は不均一で脱落しやすく、弱い膜であつ
た。
[Technical Field] The present invention relates to an improved electrolytic oxidative polymerization method for heterocyclic compounds. [Prior Art and its Problems] It has been known that a polymer film can be obtained on an electrically conductive electrode substrate by electrolytically oxidizing and polymerizing a heterocyclic compound or the like in an organic solvent. These polymers exhibit various electroactivities and are considered promising materials for new electrodes for batteries, electrochemical sensors, electrochromic displays, etc. However, polymer films obtained by conventional methods have problems with surface smoothness, adhesion with electrode substrates, etc., and it has been difficult to obtain stable characteristics. [Object of the Invention] An object of the present invention is to provide an electrolytic oxidative polymerization method for obtaining a polymer film of a heterocyclic compound having excellent surface smoothness and adhesion to an electrode substrate. [Structure of the Invention] The present invention provides an improved electrolytic polymerization method characterized in that an amine is added during electrolytic oxidative polymerization of a heterocyclic compound selected from pyrrole, indole, carbazole, dibenzofuran, and dibezothiophene in an organic solvent. This invention relates to an oxidative polymerization method. In the present invention, electrolytic oxidation polymerization is carried out using an apparatus as shown in FIG. This is called a three-electrode electrolytic cell, which is very commonly used when performing electrolytic reactions, and does not necessarily require a glass filter between each chamber. By injecting an electrolytic oxidation polymerization solution into this electrolytic cell and applying a predetermined voltage between the working electrode and the counter electrode, a polymerization reaction is started and a polymer film is formed on the working electrode. The thickness of the membrane (the amount of polymer) is adjusted by the amount of electricity applied. The magnitude of the voltage applied between the two electrodes can be determined to be the most efficient value by measuring the voltage-current characteristics of the electrolytically oxidized polymerization solution. An electrically conductive material such as platinum, carbon, Nesa glass, or stainless steel is used for the working electrode and the counter electrode. In this case, higher efficiency can be obtained if the surface area of the counter electrode is as large as possible. The reference electrode is a potassium chloride saturated calomel electrode.
A sodium chloride saturated calomel electrode, a silver/silver chloride electrode, etc. that can provide a reference potential are used, but depending on the type of supporting electrolyte in the electrolytic oxidation polymerization solution used, they may react with the internal solution of the electrode and cause precipitates. In such cases, it is necessary to select an appropriate one. The electrolytic oxidation polymerization solution used in the present invention is prepared by dissolving a heterocyclic compound as a polymerization monomer, a supporting electrolyte, and an amine additive in an organic solvent. Nitrogen gas is bubbled through this solution for 10 to 20 minutes before it is used for the reaction. Supporting electrolytes include lithium perchlorate, sodium perchlorate, sodium sulfate, tetraalkylammonium tetrafluoroborate, sodium trifluoroacetate, etc., but they are soluble in the solvent used and are compatible with polymeric monomers and additives. Requires no reaction. The amount added is usually about 0.1 mol/. The organic solvent that can be used in the present invention is not particularly limited as long as it can dissolve all of the polymerized monomer, supporting electrolyte, and amine additive. Specific examples include acetonitrile, tetrahydrofuran, propylene carbonate, and benzonitrile. The amine additive used in the present invention is not particularly limited as long as it does not undergo electrolytic oxidation polymerization, but specific examples include methylamine, ethylamine, dimethylamine, trimethylamine, allylamine, cyclohexylamine, pyridine, pyrazine, and quinoline. It will be done. The amount of these additives is preferably in the range of 0.1 mol to 5.0 mol per 1 mol of polymerized monomer, and addition of 5.0 mol or more inhibits the polymerization reaction. The amount of additive to the reaction solvent is preferably in the range of 0.01 to 10.0 mol/. [Effects of the Invention] The polymer film obtained using the present invention has superior uniformity, surface smoothness, and adhesion to the electrode substrate compared to conventional ones, and this makes it possible to obtain stable and stable polymer films in practical use. There are effects such as improved performance. EXAMPLES The present invention will be explained in more detail with reference to Examples below. Examples 1 to 3 Electrolytic oxidative polymerization was carried out using the apparatus shown in FIG.
The working electrode has a size of 1 x 4 cm, a thickness of 1 mm, and a surface resistance of 10.
Ω indium oxide Nesaglass was used and installed so that the contact area with the electrolytic oxidation polymerization solution was 2 cm 2 . A platinum plate with a thickness of 0.1 mm and a surface area of 15 cm 2 was used as the counter electrode. A sodium chloride saturated calomel electrode was used as the reference electrode. The electrolytic oxidation polymerization solution contains 0.67 g (0.1 mol/) of pyrrole and 2.45 g (0.2 mol/) of sodium perchlorate.
), pyridine 0.79g (0.1mol/) ~ 3.16g
(0.4 mol/) was dissolved in acetonitrile to make a total volume of 100 ml. Addition amount of pyridine is 0.1
Example 1 was determined to be 0.2 mol/mole, and Example 3 was 0.4 mol/mole/mole/mole. After bubbling nitrogen gas into each of these solutions for 15 minutes, they were poured into a three-electrode electrolytic cell. Each to the working electrode
Polymerization is started by applying a voltage of 1.1V, and the amount of current applied is
The reaction was terminated when the temperature reached 0.2 coulombs/cm 2 . The polymer film formed on the working electrode was washed with acetonitrile and dried before being used for evaluation. A thin film profilometer was used to measure the film thickness and surface smoothness. The measurement results of Examples 1 to 3 were as shown in Table 1. Here, R is the pyridine addition rate and represents the molar ratio of monomer to pyridine. T 1 and T 2 represent the film thickness 9 and the surface protrusion 10, respectively, as shown in FIG. Therefore, the smaller the value of the surface protrusion T 2 , the more smooth the film surface becomes. Comparative example 1 Not adding pyridine and reducing the applied voltage
The same method as in Example 1 was carried out except that the voltage was 0.9V. The properties of the obtained membrane were as shown in Table 1. Pyridine addition rate R, film thickness T 1 and surface protrusion T 2
3 and 4 respectively, and the characteristics of the film of Comparative Example 1 are B in the diagram.
Represented by points. On the other hand, the characteristics of the films obtained in Examples 1 to 3 are expressed by P 1 to P 3 points, respectively.
The results show that although the film thickness tends to decrease slightly by adding pyridine, the surface smoothness of the film is dramatically improved. It was also observed that the addition of pyridine improved the adhesion of the polymer film to the electrode substrate. That is, when the electrode with the polymer film attached was immersed in water for several minutes and then dried several times, the electrode obtained in Comparative Example 1 was completely peeled off, but in Examples 1 to 3, it was completely peeled off. None of the results were changed. Example 4 Electrolytic oxidation polymerization solution contains 1.86 g of dibenzothiophene
(0.1 mol/), sodium perchlorate 2.45 g (0.2
2.37 g (0.3 mol/) of pyridine was dissolved in acetonitrile to make a total volume of 100 ml. Polymerization was started by applying a voltage of 2.2 V to the working electrode, and the reaction was terminated when the amount of current applied reached 0.50 coulombs/cm 2 . Other operations were performed in the same manner as in Example 1. The obtained polymer film adhered uniformly to the electrode substrate. The measurement results of the film properties were as shown in Table 1. Comparative Example 2 The same procedure as Example 4 was carried out except that pyridine was not added. Almost no polymer adhered to the electrode. Example 5 The same procedure as in Example 4 was carried out except that 1.17 g (0.1 mol/) of indole was used as the monomer and the applied voltage was 2.0V. A uniform polymer film was obtained. The properties of the membrane were as shown in Table 1. Comparative Example 3 No pyridine was added and the applied voltage was
The same procedure as in Example 5 was carried out except that the voltage was set to 1.35V. Although polymer was produced, most of it fell off from the electrode substrate. Example 6 The electrolytic oxidation polymerization solution contained 0.84 g of carbazole (0.05 g
mol/), 7.74 g (0.2 mol/) of tetrabutylammonium hexafluorophosphate, and 1.19 g (0.15 mol/) of pyridine were dissolved in acetonitrile to make a total volume of 100 ml. Polymerization was initiated by applying a voltage of 2.5 V to the working electrode, and the reaction was terminated 10 minutes later. Other operations were performed in the same manner as in Example 1. A uniform polymer film was obtained. The properties of the membrane were as listed in Table 1. Comparative Example 4 The same procedure as Example 6 was carried out except that pyridine was not added. The polymer did not adhere uniformly to the electrode substrate. The membrane properties are shown in Table 1. Example 7 0.84 g of dibenzofuran (0.05 mol/
) and the applied voltage was 3.5V. A uniform and shiny polymer film was obtained. The membrane properties are shown in Table 1. Comparative Example 5 The same procedure as Example 7 was carried out except that pyridine was not added. The polymer was non-uniform and easily fell off, resulting in a weak film.

【表】【table】

【表】 *印:重合体と電極基板との密着性が弱く満足な膜が
得られないため評価できない。
表1の実施例から明らかなように、有機溶媒中
での複素環式化合物の電解酸化重合において、ア
ミンを添加した場合に得られる重合体膜は、表面
突起T2の値が小さい。すなわち表面平滑性に優
れている。 一方、アミンを添加しない比較例では表面平滑
性が悪いばかりでなく、電極基板との密着性が弱
いため満足な重合体膜を形成することが困難であ
る。
[Table] *Marked: Cannot be evaluated because the adhesion between the polymer and the electrode substrate is weak and a satisfactory film cannot be obtained.
As is clear from the examples in Table 1, the polymer film obtained when an amine is added in the electrolytic oxidative polymerization of a heterocyclic compound in an organic solvent has a small value of surface protrusions T 2 . In other words, it has excellent surface smoothness. On the other hand, in a comparative example in which no amine was added, not only the surface smoothness was poor, but also the adhesion to the electrode substrate was weak, making it difficult to form a satisfactory polymer film.

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

第1図は、本発明で用いた三電極式電解酸化重
合槽を示し、第2図は評価に用いた重合体膜の拡
大断面図を示す。 1は動作電極、2は対極、3は基準電極、4は
ガラスフイルター、5は電解酸化重合液、6は重
合体膜、7は電極基板、8は膜厚を測定するため
に機械的に膜を剥離した部分、9は膜厚T1、1
0は表面突起T2である。 第3図は、ピロールの電解酸化重合で得られた
重合体膜の厚さとピリジン添加量との関係を示
し、第4図は、ピロールの重合体膜の表面突起と
ピリジン添加量との関係を示す。P1〜P3は各々
実施例1〜3で得られたもの、Bは比較例1で得
られたものである。
FIG. 1 shows the three-electrode electrolytic oxidation polymerization tank used in the present invention, and FIG. 2 shows an enlarged sectional view of the polymer membrane used for evaluation. 1 is a working electrode, 2 is a counter electrode, 3 is a reference electrode, 4 is a glass filter, 5 is an electrolytic oxidation polymerization solution, 6 is a polymer film, 7 is an electrode substrate, and 8 is a mechanical membrane for measuring film thickness. 9 is the film thickness T 1 , 1
0 is the surface protrusion T2 . Figure 3 shows the relationship between the thickness of the polymer film obtained by electrolytic oxidative polymerization of pyrrole and the amount of pyridine added, and Figure 4 shows the relationship between the surface protrusions of the pyrrole polymer film and the amount of pyridine added. show. P 1 to P 3 were obtained in Examples 1 to 3, respectively, and B was obtained in Comparative Example 1.

Claims (1)

【特許請求の範囲】 1 ピロール、インドール、カルバゾール、ジベ
ンゾフランおよびジベンゾチオフエンから選ばれ
た複素環式化合物の有機溶媒中での電解酸化重合
に際し、アミンを添加することを特徴とする電解
酸化重合方法。 2 アミンがメチルアミン、エチルアミン、ジメ
チルアミン、トリメチルアミン、アリルアミン、
シクロヘキシルアミン、ピリジン、ピラジンまた
はキノリンである特許請求の範囲第1項記載の電
解酸化重合方法。 3 アミンの添加量が複素環式化合物1モルに対
し0.1〜5モルである特許請求の範囲第1項記載
の電解酸化重合方法。
[Scope of Claims] 1. An electrolytic oxidative polymerization method characterized in that an amine is added during the electrolytic oxidative polymerization of a heterocyclic compound selected from pyrrole, indole, carbazole, dibenzofuran, and dibenzothiophene in an organic solvent. . 2 The amine is methylamine, ethylamine, dimethylamine, trimethylamine, allylamine,
The electrolytic oxidative polymerization method according to claim 1, wherein cyclohexylamine, pyridine, pyrazine or quinoline is used. 3. The electrolytic oxidative polymerization method according to claim 1, wherein the amount of the amine added is 0.1 to 5 mol per mol of the heterocyclic compound.
JP7867984A 1984-04-20 1984-04-20 Electrolytic oxidation polymerization Granted JPS60223817A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7867984A JPS60223817A (en) 1984-04-20 1984-04-20 Electrolytic oxidation polymerization

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7867984A JPS60223817A (en) 1984-04-20 1984-04-20 Electrolytic oxidation polymerization

Publications (2)

Publication Number Publication Date
JPS60223817A JPS60223817A (en) 1985-11-08
JPH0578575B2 true JPH0578575B2 (en) 1993-10-29

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP7867984A Granted JPS60223817A (en) 1984-04-20 1984-04-20 Electrolytic oxidation polymerization

Country Status (1)

Country Link
JP (1) JPS60223817A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62270621A (en) * 1985-12-06 1987-11-25 Showa Denko Kk Polymer having isoindole structure and its production
GB9425207D0 (en) * 1994-12-14 1995-02-15 Aromascan Plc Semi-conducting organic polymers
JP4595708B2 (en) * 2005-06-27 2010-12-08 住友化学株式会社 Process for producing aromatic polymer

Also Published As

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JPS60223817A (en) 1985-11-08

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