JP2650777B2 - Method for producing polyaniline - Google Patents
Method for producing polyanilineInfo
- Publication number
- JP2650777B2 JP2650777B2 JP2260887A JP26088790A JP2650777B2 JP 2650777 B2 JP2650777 B2 JP 2650777B2 JP 2260887 A JP2260887 A JP 2260887A JP 26088790 A JP26088790 A JP 26088790A JP 2650777 B2 JP2650777 B2 JP 2650777B2
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- Japan
- Prior art keywords
- polyaniline
- mol
- film
- concentration
- electrolytic
- 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
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- Macromolecular Compounds Obtained By Forming Nitrogen-Containing Linkages In General (AREA)
- Electrochromic Elements, Electrophoresis, Or Variable Reflection Or Absorption Elements (AREA)
- Polymers With Sulfur, Phosphorus Or Metals In The Main Chain (AREA)
Description
【発明の詳細な説明】 [産業上の利用分野] 本発明はエレクトロクロミック表示素子の発色電極な
どとして有用なポリアニリンの製造方法に関する。Description: TECHNICAL FIELD The present invention relates to a method for producing polyaniline useful as a color-forming electrode of an electrochromic display element.
[従来の技術] 白金や金などの金属電極上にポリアニリンを電析させ
る場合には均一な膜を得ることが比較的容易であるが、
ITO膜、NESA膜などの透明導電膜上にポリアニリンを電
析させる場合には、アニリンモノマーと酸性水溶液の濃
度がそれぞれ1モル/程度では付着が可能であるが、
充分な膜厚のポリアニリンを合成することが困難であ
り、また、濃度を低くして、長時間重合させるとポリア
ニリンが透明導電膜上に微粉化されて堆積し、均一な膜
を得ることが困難であった。また、濃度をさらに高くす
ると重合されたポリアニリンが電解液に溶解して剥離し
てしまうという問題点があった。[Prior art] When depositing polyaniline on a metal electrode such as platinum or gold, it is relatively easy to obtain a uniform film,
In the case of depositing polyaniline on a transparent conductive film such as an ITO film or a NESA film, it is possible to adhere at a concentration of about 1 mol / each of the aniline monomer and the acidic aqueous solution.
It is difficult to synthesize a polyaniline having a sufficient film thickness, and when polymerizing for a long time at a low concentration, polyaniline is pulverized and deposited on the transparent conductive film, and it is difficult to obtain a uniform film. Met. Further, when the concentration is further increased, there is a problem that the polymerized polyaniline dissolves in the electrolytic solution and peels off.
[発明の目的] 本発明はこのような点に鑑みてなされたものであり、
均一な製膜が困難とされる透明導電膜上に均一で付着力
の強いポリアニリン膜を製造する方法を提供することを
目的とする。[Object of the Invention] The present invention has been made in view of the above points,
An object of the present invention is to provide a method for producing a polyaniline film having a uniform and strong adhesive force on a transparent conductive film where uniform film formation is difficult.
[問題点を解決するための手段] 本発明は、アニリンモノマーと酸性水溶液を混合した
電解液に、透明導電膜が形成された基板を浸漬し、該基
板を一方の電極として電解酸化重合法により前記透明導
電膜上にボリアニリンを製造する方法において、まず、
アニリンモノマー濃度を0.1〜1.0モル/の範囲、酸性
水溶液の濃度を0.1〜1.0モル/の範囲、電流密度を10
μA/cm2〜1mA/cm2なる条件で100〜700Åのポリアニリン
を電解酸化重合し、その後、酸性水溶液の濃度を0.1〜
1.0モル/の範囲、アニリンモノマーの濃度を0.1〜1.
0モル/の範囲とする電解液により、さらに電解酸化
重合するようにしたことを特徴とする。[Means for Solving the Problems] In the present invention, a substrate on which a transparent conductive film is formed is immersed in an electrolytic solution obtained by mixing an aniline monomer and an acidic aqueous solution, and the substrate is used as one electrode by electrolytic oxidation polymerization. In the method for producing boraniline on the transparent conductive film, first,
The aniline monomer concentration is in the range of 0.1-1.0 mol /, the concentration of the acidic aqueous solution is in the range of 0.1-1.0 mol /, and the current density is 10
Under the condition of μA / cm 2 -1 mA / cm 2 , 100-700 ポ リ of polyaniline is subjected to electrolytic oxidation polymerization, and then the concentration of the acidic aqueous solution is adjusted to 0.1-
1.0 mol / range, aniline monomer concentration 0.1-1.
It is characterized in that electrolytic oxidative polymerization is further performed with an electrolytic solution having a range of 0 mol /.
[作用] 本発明者らは一回の電解酸化重合では、1,000Å以上
の均一な膜を透明導電膜上に製造することは困難である
が、特定条件のもとで二回電解酸化重合を行うというこ
とに着目して本発明をなすに到ったものである。[Operation] The present inventors have found that it is difficult to produce a uniform film of 1,000 mm or more on a transparent conductive film by a single electrolytic oxidation polymerization. The present invention has been accomplished by paying attention to performing the method.
すなわち、まず、アニリンモノマー濃度を0.1〜1.0モ
ル/の範囲、酸性水溶液の濃度を0.1〜1.0モル/の
範囲、電流密度を10μA/cm2〜1mA/cm2なる条件で100〜7
00Åのポリアニリンを電解酸化重合するものである。こ
のとき、アニリンモノマー濃度がこの範囲より小さいと
良好なポリアニリン膜を得ることは困難であり、しかも
重合に要する時間がかかり過ぎ、この範囲より大きい場
合にはアニリンモノマーが電解液に溶解しにくくなる難
点がある。酸性水溶液の濃度がこの範囲より小さいと電
解液の電気抵抗が大きくなり、ポリアニリンが製膜され
る陽極の電位が上昇するのでポリアニリンが分解してし
まう恐れがあり、この範囲により大きいとITO膜などの
透明導電膜が溶解する恐れがある。電流密度がこの範囲
より小さい場合には、重合に要する時間がかかり過ぎ、
この範囲より大きい場合には、均一な膜を重合するのが
困難である。That is, first, the aniline monomer concentration is in the range of 0.1 to 1.0 mol /, the concentration of the acidic aqueous solution is in the range of 0.1 to 1.0 mol /, and the current density is 10 μA / cm 2 to 1 mA / cm 2.
In this method, polyaniline of 00% is subjected to electrolytic oxidation polymerization. At this time, if the aniline monomer concentration is less than this range, it is difficult to obtain a good polyaniline film, and it takes too much time for polymerization.If the aniline monomer concentration is more than this range, the aniline monomer is difficult to dissolve in the electrolytic solution. There are difficulties. If the concentration of the acidic aqueous solution is smaller than this range, the electric resistance of the electrolytic solution increases, and the potential of the anode on which the polyaniline is formed increases, so that polyaniline may be decomposed. May be dissolved. If the current density is less than this range, it takes too much time for polymerization,
If it is larger than this range, it is difficult to polymerize a uniform film.
また、膜厚が100Åより小さいと、膜厚制御が困難で
あり、700Åより大きいと、膜厚の不均一性が次第に増
大される。When the film thickness is smaller than 100 °, it is difficult to control the film thickness. When the film thickness is larger than 700 °, the nonuniformity of the film thickness is gradually increased.
このような条件で電着時間を10分以内として、電解重
合を行って、洗浄すると表層の付着力の弱いポリニアリ
ンが落とされ、その結果100〜700Åの厚さの比較的均一
なポリアニリン膜が製膜される。Under such conditions, the electrodeposition time is set to 10 minutes or less, electrolytic polymerization is performed, and when washed, polyniarin having a weak surface adhesion is dropped, and as a result, a relatively uniform polyaniline film having a thickness of 100 to 700 mm is produced. Filmed.
次に、酸性水溶液の濃度を0.1〜1.0モル/の範囲、
アニリンモノマーの濃度を0.1〜1.0モル/の範囲とす
る電解液により電解酸化重合すると、電流密度と電着時
間を適宜選択することにより、1,000〜5,000Åの均一な
ポリアニリン膜を製膜することができるものである。Next, the concentration of the acidic aqueous solution is in the range of 0.1 to 1.0 mol /,
When electrolytic oxidation polymerization is carried out using an electrolytic solution having an aniline monomer concentration in the range of 0.1 to 1.0 mol /, a uniform polyaniline film of 1,000 to 5,000 mm can be formed by appropriately selecting the current density and the electrodeposition time. You can do it.
これは、一回目の電解酸化重合で製膜可能な膜厚を有
するポリアニリンを重合しておくことにより、二回目の
電解酸化重合時にポリアニリン膜が付着しやすい状態に
なっており、しかも一回目に重合されたポリアニリン膜
の表面凹凸による表面抵抗のばらつきは、透明導電膜の
表面凹凸による表面抵抗のばらつきに比較して大幅に小
さくなっているので、5,000Å程度まで厚く製膜しても
均一性が保たれることに起因するものと思われる。This is because polyaniline having a film thickness that can be formed by the first electrolytic oxidation polymerization is polymerized, so that the polyaniline film easily adheres during the second electrolytic oxidation polymerization. The variation in surface resistance due to the surface irregularities of the polymerized polyaniline film is much smaller than the variation in surface resistance due to the surface irregularities of the transparent conductive film. Is likely to be maintained.
[実施例] 以下、本発明の実施例を比較例とともに、詳細に説明
する。[Examples] Hereinafter, examples of the present invention will be described in detail along with comparative examples.
実施例1 アニリン0.1モル/と硫酸0.1モル/を混合したも
のを電解液として入れた電解槽に、ITO膜被膜の40mm角
のガラス板、白金板および飽和カロメル電極をそれぞれ
陽極、陰極、参照電極として浸漬し、直流電源に接続し
た。Example 1 A 40 mm square glass plate, a platinum plate, and a saturated calomel electrode with an ITO film coating were placed on an anode, a cathode, and a reference electrode, respectively, in an electrolytic bath containing an electrolyte containing a mixture of aniline 0.1 mol / and sulfuric acid 0.1 mol /. And connected to a DC power supply.
このような状態で、直流電源により、参照電極で陽極
電位が初期に約0.85V以上であることを確認して、電流
密度100μA/cm2(定電流)で5分間通電してポリアニリ
ン膜をITO膜上に重合した。その後、電解槽からガラス
板を取り出し水洗したところ、表層の付着力の弱いポリ
アニリンが落とされ、ITO膜上には200Å厚さのポリアニ
リン膜が製膜された。In such a state, it is confirmed that the anode potential is initially about 0.85 V or more at the reference electrode by a DC power supply, and a current density of 100 μA / cm 2 (constant current) is applied for 5 minutes to deposit the polyaniline film on the ITO. Polymerized on the membrane. Thereafter, when the glass plate was taken out of the electrolytic cell and washed with water, the polyaniline having a weak adhesive force on the surface layer was dropped, and a 200-mm-thick polyaniline film was formed on the ITO film.
次に、このガラス板をアニリン0.5モル/と硫酸0.5
モル/を混合したものを電解液として入れた電解槽に
飽和カロメル電極、参照電極とともに浸漬し、電流密度
100μA/cm2で10分間通電してポリアニリン膜を重合し
た。Next, this glass plate was treated with 0.5 mol of aniline / 0.5 mol of sulfuric acid.
Immersed together with a saturated calomel electrode and a reference electrode in an electrolytic cell containing a mixture of
Electric current was applied at 100 μA / cm 2 for 10 minutes to polymerize the polyaniline film.
このようにして得られたポリアニリン膜は2,400Åの
良質で均一性に優れたものであった。The polyaniline film thus obtained was of good quality and excellent in uniformity of 2,400 mm.
実施例1′ 実施例1で得られたポリアニリンをエレクトロクロミ
ック素子に応用した例を示す。Example 1 'An example in which the polyaniline obtained in Example 1 is applied to an electrochromic device will be described.
実施例1で得られた3mm厚さのガラス基板と、3mm厚さ
のガラス板に透明導電膜と発色層WO3が形成れた基板を
相対向させ、周辺部をシールした後、電解液として1モ
ル過塩素酸リチウムを含むプロピレンカーボネート溶液
を充填した。And glass substrates 3mm thick obtained in Example 1, 3mm was thick with a transparent conductive film on a glass plate coloring layer WO 3 formed in the opposite substrate, and after sealing the periphery, as an electrolyte A propylene carbonate solution containing 1 molar lithium perchlorate was charged.
このようにして得られたエレクトロクロミック素子に
ポリアニリンを陽極、WO3を陰極として1.0Vの直流電圧
を印加したところ、ポリアニリンとWO3が共に青色に発
色、可視光透過率が10.5%となり、良好な光遮蔽性を示
し、WO3を陽極、ポリアニリンを陰極として0.5Vの直流
電圧を印加したところ、ポリアニリン、WO3とも消色、
可視光透過率が55%となり、良好な光透過性を示した。When a DC voltage of 1.0 V was applied to the thus obtained electrochromic device using polyaniline as an anode and WO 3 as a cathode, both polyaniline and WO 3 were colored blue, and the visible light transmittance was 10.5%. When a DC voltage of 0.5 V was applied using WO 3 as an anode and polyaniline as a cathode, both polyaniline and WO 3 were decolorized.
The visible light transmittance was 55%, indicating good light transmittance.
この着消色を約2,000回繰り返しても、ポリアニリン
膜は剥離することなく、しかも、着色時に色むらを生ず
ることもなく、優れたエレクトロクロミズムを示すこと
を確認した。また、この間エレクトロクロミックミック
素子は一定電圧を印加すると、濃度の変動がきわめて小
さく一定の濃度が得られ安定した駆動を行うことができ
た。It was confirmed that the polyaniline film exhibited excellent electrochromism without being peeled off even after repeating the discoloration about 2,000 times, and without causing color unevenness upon coloring. Also, during this period, when a constant voltage was applied to the electrochromic element, the fluctuation of the density was extremely small and a constant density was obtained, so that stable driving could be performed.
これは、ポリアニリンがITO膜上に均一に重合され、
その付着力も強いことを示すものである。This is because polyaniline is uniformly polymerized on the ITO film,
This indicates that the adhesive force is also strong.
比較例 アニリン0.5モル/と硫酸0.5モル/を混合したも
のを電解液として入れた電解槽に、ITO膜被膜の40mm角
のガラス板、白金板、飽和カロメル電極をそれぞれ陽
極、陰極、参照電極として浸漬し、電流密度100μA/cm2
(定電流)で30分間通電してポリアニリン膜を重合し
て、水洗したところ、ポリアニリン膜が流出して、膜圧
が100Åを下回ってしまい、しかも均一性が損なわれ、
実用に供しうるものではなかった。Comparative Example A 40 mm square glass plate, a platinum plate, and a saturated calomel electrode of an ITO film coating were used as an anode, a cathode, and a reference electrode, respectively, in an electrolytic tank containing an electrolyte mixed with 0.5 mol / of aniline and 0.5 mol / of sulfuric acid. Immersion, current density 100μA / cm 2
(Positive current) for 30 minutes to polymerize the polyaniline film and rinse it with water, the polyaniline film flows out, the film pressure falls below 100 °, and the uniformity is impaired.
It was not practical.
実施例2 70mm角のITO膜被覆ガラス板を陽極として、二回めの
硫酸濃度を0.1モル/、通電時間を20分間とした以外
は実施例1と同じ条件でポリアニリンを重合した。Example 2 Polyaniline was polymerized under the same conditions as in Example 1 except that a 70 mm square ITO film-coated glass plate was used as an anode, the second sulfuric acid concentration was 0.1 mol /, and the energizing time was 20 minutes.
このようにして得られたポリアニリン膜は膜厚3,500
Åの均一な膜であった。The polyaniline film thus obtained has a thickness of 3,500.
Å was a uniform film.
実施例3 70mm角のITO膜被覆ガラス板を陽極として、二回めの
硫酸濃度を0.5モル/、電流密度500μA/cm2、通電時
間を4分間とした以外は実施例1と同じ条件でポリアニ
リンを重合した。Example 3 Polyaniline was prepared under the same conditions as in Example 1 except that a 70 mm square ITO-coated glass plate was used as an anode, the second sulfuric acid concentration was 0.5 mol /, the current density was 500 μA / cm 2 , and the energizing time was 4 minutes. Was polymerized.
このようにして得られたポリアニリン膜は膜厚4,500
Åの均一な膜であった。The polyaniline film thus obtained had a thickness of 4,500.
Å was a uniform film.
実施例4 70mm角のITO膜被覆ガラス板を陽極として、二回めの
アニリン濃度を0.1モル/、硫酸濃度を0.1モル/、
通電時間を10分間とした以外は実施例1と同じ条件でポ
リアリニンを合成した。Example 4 Using a 70 mm square ITO film-coated glass plate as an anode, the second aniline concentration was 0.1 mol /, the sulfuric acid concentration was 0.1 mol /,
Polyallinine was synthesized under the same conditions as in Example 1 except that the energization time was changed to 10 minutes.
このようにして得られたポリアニリン膜は膜厚2,400
Åの均一な膜であった。The polyaniline film thus obtained has a thickness of 2,400.
Å was a uniform film.
実施例5 一回目のアニリン濃度を0.3モル/、硫酸濃度を0.5
モル/、電流密度500μA/cm2(定電流)、通電時間を
3分間として、二回目のアニリン濃度を0.3モル/、
硫酸濃度を0.5モル/、通電時間を5分間とした以外
は実施例1と同じ条件でポリアニリンを重合した。Example 5 The first aniline concentration was 0.3 mol / and the sulfuric acid concentration was 0.5
Mol /, current density 500 μA / cm 2 (constant current), energizing time 3 minutes, the second aniline concentration 0.3 mol /,
Polyaniline was polymerized under the same conditions as in Example 1 except that the sulfuric acid concentration was 0.5 mol / hour and the energizing time was 5 minutes.
このようにして得られたポリアニリン膜は膜厚1,500
Åの均一な膜であった。The polyaniline film thus obtained has a thickness of 1,500.
Å was a uniform film.
なお、一回目の電解重合によって得られたポリアニリ
ンの膜厚は600Åであった。The thickness of the polyaniline obtained by the first electrolytic polymerization was 600 °.
実施例6 一回目のアニリン濃度を0.5モル/、硫酸濃度を0.5
モル/、電流密度を50μA/cm2(定電流)、通電時間
を10分間とし、二回目のアニリン濃度を0.3モル/、
硫酸濃度を0.5モル/、通電時間を5分間とした以外
は実施例1と同じ条件でポリアニリンを重合した。Example 6 The first aniline concentration was 0.5 mol /, and the sulfuric acid concentration was 0.5
Mol /, the current density was 50 μA / cm 2 (constant current), the energization time was 10 minutes, and the second aniline concentration was 0.3 mol /
Polyaniline was polymerized under the same conditions as in Example 1 except that the sulfuric acid concentration was 0.5 mol / hour and the energizing time was 5 minutes.
このようにして得られたポリアニリン膜は膜厚2,400
Åの均一な膜であった。The polyaniline film thus obtained has a thickness of 2,400.
Å was a uniform film.
なお、一回目の電解重合によって得られたポリアニリ
ンの膜厚は200Åであった。The thickness of the polyaniline obtained by the first electrolytic polymerization was 200 °.
実施例7 アニリン0.1モル/とHBF40.2モル/を混合したも
のを電解液として入れた電解槽に、ITO膜被覆の40mm角
のガラス板、白金板および飽和カロメル電極をそれぞれ
陽極、陰極、参照電極として浸漬し、電流密度50μA/cm
2(定電流)で5分間通電してポリアニリン膜を重合
し、水洗後、このガラス板をアニリン0.5モル/と、H
BF41.0モル/を混合したものを電解液として入れた電
解槽に飽和カロメル電極、参照電極とともに浸漬し、電
流密度1.0mA/cm2で5分間通電してポリアニリン膜を重
合した。このようにして得られたポリアリニン膜は4500
Åの良質で均一性に優れたものであった。Example 7 A 40 mm square glass plate, a platinum plate, and a saturated calomel electrode each coated with an ITO film were placed in an electrolytic cell containing an electrolytic solution containing 0.1 mol / of aniline and 0.2 mol / of HBF 4 as an anode, a cathode and a reference, respectively. Immerse as an electrode, current density 50μA / cm
2 Apply a current (constant current) for 5 minutes to polymerize the polyaniline film. After washing with water, the glass plate was treated with 0.5 mol / ml of aniline and H
A saturated calomel electrode and a reference electrode were immersed in an electrolytic tank containing a mixture of 1.0 mol / BF 4 as an electrolytic solution, and a current density of 1.0 mA / cm 2 was supplied for 5 minutes to polymerize the polyaniline film. The polyallynin film obtained in this way is 4500
Å was of good quality and excellent in uniformity.
以上、好適な実施例により説明したが、本発明はこれ
に限定されるものではなく種々の応用が可能である。The preferred embodiment has been described above, but the present invention is not limited to this, and various applications are possible.
酸性水溶液として使用する酸は、硫酸、HBF4(四フッ
化ホウ素酸)以外にも、過塩素酸、塩酸等の無機酸の1
種または2種以上を組合せて使用することができる。Acids used as the acidic aqueous solution include inorganic acids such as perchloric acid and hydrochloric acid in addition to sulfuric acid and HBF 4 (boron tetrafluoride).
Species or a combination of two or more can be used.
また、酸性水溶液として硫酸を使用する場合に一回目
の電解重合時のアニリンモノマー濃度と硫酸の濃度は0.
1〜1.0モル/の範囲内で適宜選択すればよいが、特に
硫酸濃度をxモル/とすれば、アニリンモノマー濃度
は(0.1x+0.05)モル/以上とした方がよいことを確
認した。硫酸は電解液の中でイオン化しており、このイ
オンによって電気を導くものであるから、硫酸濃度が高
いと電解液の抵抗が低くなり、そのために陽極電位が低
くなって電解重合に必要な初期電位(約0.85V)を下回
るとポリアニリンの重合ができない。しかしながら、硫
酸濃度が高くても、アニリンモノマーの濃度が高くなる
と、このアニリンモノマーが電解液中のイオン(水素イ
オン、硫酸イオン)の動きを妨げるので、電解液の抵抗
が高くなり、同時に陽極電位も高くなり、ポリアニリン
の合成が可能になる。Also, when sulfuric acid is used as the acidic aqueous solution, the aniline monomer concentration and the sulfuric acid concentration at the time of the first electrolytic polymerization are 0.
The concentration may be appropriately selected within the range of 1 to 1.0 mol /, and it has been confirmed that, particularly when the sulfuric acid concentration is x mol /, the aniline monomer concentration should be (0.1x + 0.05) mol / or more. Sulfuric acid is ionized in the electrolytic solution and conducts electricity by these ions.If the sulfuric acid concentration is high, the resistance of the electrolytic solution decreases, and the anodic potential decreases. When the potential is lower than about 0.85V, polyaniline cannot be polymerized. However, even if the sulfuric acid concentration is high, when the concentration of the aniline monomer increases, the aniline monomer hinders the movement of ions (hydrogen ions, sulfate ions) in the electrolytic solution, so that the resistance of the electrolytic solution increases and, at the same time, the anode potential And the synthesis of polyaniline becomes possible.
[発明の効果] 本発明によれば、特定条件で二回の電解酸化重合を行
うことにより、従来困難であったITO膜、NESA膜などの
透明導電膜上にポリアニリンを合成・製膜することがで
き、膜厚も均一で、付着力も強いので、エレクトロクロ
ミック材とし特に好適に応用することができるのは勿
論、エレクトロクロミック素子の補助電極などの各種の
電子材料として使用することができるものである。[Effects of the Invention] According to the present invention, polyaniline is synthesized and formed on a transparent conductive film such as an ITO film or a NESA film, which was conventionally difficult, by performing electrolytic oxidation polymerization twice under specific conditions. Can be used as various kinds of electronic materials such as auxiliary electrodes of an electrochromic element, as well as being particularly suitable as an electrochromic material because of its uniform thickness and strong adhesion. It is.
フロントページの続き (56)参考文献 特開 昭60−253021(JP,A) 特開 平2−79047(JP,A) 特開 昭57−11810(JP,A) 特開 昭57−145019(JP,A) 特開 昭60−91528(JP,A) 特公 平5−16364(JP,B2)Continuation of front page (56) References JP-A-60-253021 (JP, A) JP-A-2-79047 (JP, A) JP-A-57-11810 (JP, A) JP-A-57-145019 (JP) , A) JP-A-60-91528 (JP, A) JP-B-5-16364 (JP, B2)
Claims (1)
電解液に、透明導電膜が形成された基板を浸漬し、該基
板を一方の電極として電解酸化重合法により前記透明導
電膜上にボリアニリンを製造する方法において、まず、
アニリンモノマー濃度を0.1〜1.0モル/の範囲、酸性
水溶液の濃度を0.1〜1.0モル/の範囲、電流密度を10
μA/cm2〜1mA/cm2なる条件で100〜700Åのポリアニリン
を電解酸化重合し、その後、酸性水溶液の濃度を0.1〜
1.0モル/の範囲、アニリンモノマーの濃度を0.1〜1.
0モル/の範囲とする電解液により、さらに電解酸化
重合するようにしたことを特徴とするポリアニリンの製
造方法。1. A substrate on which a transparent conductive film is formed is immersed in an electrolytic solution in which an aniline monomer and an acidic aqueous solution are mixed, and boraniline is produced on the transparent conductive film by electrolytic oxidation polymerization using the substrate as one electrode. In the method, first,
The aniline monomer concentration is in the range of 0.1-1.0 mol /, the concentration of the acidic aqueous solution is in the range of 0.1-1.0 mol /, and the current density is 10
Under the condition of μA / cm 2 -1 mA / cm 2 , 100-700 ポ リ of polyaniline is subjected to electrolytic oxidation polymerization, and then the concentration of the acidic aqueous solution is adjusted to 0.1-
1.0 mol / range, aniline monomer concentration 0.1-1.
A method for producing polyaniline, wherein electrolytic oxidation polymerization is further performed with an electrolytic solution having a range of 0 mol /.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2260887A JP2650777B2 (en) | 1990-09-29 | 1990-09-29 | Method for producing polyaniline |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2260887A JP2650777B2 (en) | 1990-09-29 | 1990-09-29 | Method for producing polyaniline |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04139214A JPH04139214A (en) | 1992-05-13 |
JP2650777B2 true JP2650777B2 (en) | 1997-09-03 |
Family
ID=17354134
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2260887A Expired - Lifetime JP2650777B2 (en) | 1990-09-29 | 1990-09-29 | Method for producing polyaniline |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2650777B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113277518A (en) * | 2021-04-27 | 2021-08-20 | 郑州市博卓科技有限公司 | Silica raw material and preparation method thereof |
-
1990
- 1990-09-29 JP JP2260887A patent/JP2650777B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH04139214A (en) | 1992-05-13 |
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