JPH0539376A - Continuous production of composite conductive polymer film - Google Patents
Continuous production of composite conductive polymer filmInfo
- Publication number
- JPH0539376A JPH0539376A JP19437091A JP19437091A JPH0539376A JP H0539376 A JPH0539376 A JP H0539376A JP 19437091 A JP19437091 A JP 19437091A JP 19437091 A JP19437091 A JP 19437091A JP H0539376 A JPH0539376 A JP H0539376A
- Authority
- JP
- Japan
- Prior art keywords
- conductive polymer
- tube
- film
- solution
- semipermeable membrane
- 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
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- Coating Of Shaped Articles Made Of Macromolecular Substances (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は導電性高分子複合膜を簡
単な操作により連続的に製造する方法の改良に関するも
のである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an improvement in a method for continuously producing a conductive polymer composite membrane by a simple operation.
【0002】[0002]
【従来の技術】近時、π共役系電子構造を特徴とする導
電性高分子は、新規な導電性材料として注目を集めてお
り、種々の分野に応用されつつある。その中で膜状に成
形した導電性高分子を機能性材料として使用せんとする
研究が盛んに行われており、これに伴って導電性高分子
の製膜方法に関し、多大に研究が行われている。2. Description of the Related Art Recently, a conductive polymer having a π-conjugated electronic structure has been attracting attention as a new conductive material and is being applied to various fields. Among them, much research is being conducted on the use of conductive polymers formed into a film as a functional material, and along with this, a great deal of research has been conducted on the method for forming conductive polymers. ing.
【0003】而して、従来の導電性高分子の製膜方法と
しては、下記の如き方法が知られている。The following methods are known as conventional film forming methods for conductive polymers.
【0004】(1)電解重合法により平板状の電極に導
電性高分子を析出せしめ導電性高分子膜の製膜を重合反
応と同時に行って製造する。(1) A conductive polymer is deposited on a flat electrode by an electrolytic polymerization method to form a conductive polymer film at the same time as a polymerization reaction.
【0005】(2)可溶可融性導電性高分子を用い、L
B法、スピンコート法、塗布乾燥法により製造する。(2) Using a soluble and fusible conductive polymer, L
It is manufactured by the B method, the spin coating method, and the coating and drying method.
【0006】(3)プラズマCVDを用いて製造する。(3) It is manufactured by using plasma CVD.
【0007】(4)スプレー噴霧式により既製膜にコー
トして製造する。(4) It is manufactured by coating a ready-made film by a spray atomization method.
【0008】然しながら、上記(1),(2)及び
(3)の方法では連続的に且つ広大な面積の導電性膜を
製造することが出来ない、又(4)の方法においては均
質的な膜をうることが出来ない。更にこれらの方法は何
れも作業性が困難であり、簡単に製造することが出来な
いのである。However, the methods (1), (2) and (3) cannot continuously produce a conductive film having a large area, and the method (4) is uniform. I can't get the film. Furthermore, all of these methods are difficult to work with and cannot be easily manufactured.
【0009】最近これらの方法の改良として導電性高分
子複合膜を隔膜法により製造する方法が開発されてい
る。即ちアニリン塩酸塩水溶液をセロハン膜にて被包
し、これをFeCl3 の水溶液中に浸漬せしめて該セロ
ハン膜の表裏にポリアニリン膜を生成させて、導電性高
分子複合膜を容易に製造する方法を開発した(Pol
y,Prep.Jpn,Vol.40,No.3(19
91),1046)。Recently, as an improvement of these methods, a method of producing a conductive polymer composite membrane by a diaphragm method has been developed. That is, a method for easily producing a conductive polymer composite film by encapsulating an aqueous solution of aniline hydrochloride with a cellophane film and immersing it in an aqueous solution of FeCl 3 to form polyaniline films on the front and back of the cellophane film. Was developed (Pol
y, Prep. Jpn, Vol. 40, No. 3 (19
91), 1046).
【0010】この方法によりえたアニリン膜は、該アニ
リン膜の間にセロハン膜が入っているために強度に優れ
且ポリアニリンはセロハン膜に強固に密着しているため
摩擦するもポリアニリンが剥離することがなく、且アニ
リン膜は上記の如くFeCl3 水溶液中に数時間放置す
るのみでよいから、煩雑な操作を必要とせず強度に優れ
たポリアニリン複合膜をうることが出来る。The aniline film obtained by this method is excellent in strength because the cellophane film is inserted between the aniline films, and the polyaniline is firmly adhered to the cellophane film, so that the polyaniline can be peeled off even if it is rubbed. Since the aniline film does not need to be left in the FeCl 3 aqueous solution for several hours as described above, a polyaniline composite film having excellent strength can be obtained without requiring complicated operations.
【0011】然しながらこの方法はセロハンチューブ内
にアニリン塩酸塩水溶液を封入して行うために製造され
る複合膜の大きさは上記チューブの大きさに限定される
と共に連続的に製造することが出来ないという問題があ
った。However, according to this method, the size of the composite membrane produced by encapsulating the aqueous solution of aniline hydrochloride in the cellophane tube is limited to the size of the tube and cannot be continuously produced. There was a problem.
【0012】[0012]
【発明が解決しようとする課題】本発明はかかる欠点を
改善せんとして鋭意研究を行った結果、導電性高分子複
合膜を連続的にしかも簡単な操作により製造する方法を
開発したものである。DISCLOSURE OF INVENTION Problems to be Solved by the Invention As a result of intensive studies aimed at remedying such drawbacks, the present invention has developed a method for producing a conductive polymer composite membrane continuously and by a simple operation.
【0013】[0013]
【課題を解決するための手段】本発明は導電性高分子モ
ノマー溶液を封入せる半透膜製チューブを、触媒溶液中
に所定速度で走行せしめつつ、該チューブの両面に導電
性高分子膜を形成せしめた後、該チューブを長手方向に
切り開き、引続き水洗及び乾燥を行うことを特徴とする
ものである。According to the present invention, a semipermeable membrane tube enclosing a conductive polymer monomer solution is run in a catalyst solution at a predetermined speed, and a conductive polymer membrane is formed on both sides of the tube. After being formed, the tube is cut open in the longitudinal direction, followed by washing with water and drying.
【0014】即ち、本発明方法は隔膜法を用いて導電性
高分子複合膜を作製し、半透膜を連続的に供給すること
により、膜厚の均一な導電性高分子複合膜を連続的にし
かも簡単な方法にて製造せんとするものである。That is, in the method of the present invention, a conductive polymer composite film is produced by using a diaphragm method, and a semipermeable membrane is continuously supplied to continuously form a conductive polymer composite film having a uniform thickness. Moreover, it is intended to be manufactured by a simple method.
【0015】[0015]
【作用】本発明において導電性高分子モノマーとしては
アニリン又はその誘導体、ピロール又はその誘導体、チ
オフェン又はその誘導体芳香族化合物等を使用するもの
であり、又、この導電性高分子モノマーを溶液とするた
めの溶媒としては水、アセトニトリル、クロロホルム等
を使用するものである。In the present invention, as the conductive polymer monomer, aniline or its derivative, pyrrole or its derivative, thiophene or its derivative aromatic compound, etc. are used, and this conductive polymer monomer is used as a solution. Water, acetonitrile, chloroform or the like is used as a solvent for the above.
【0016】なお、上記溶液の濃度は高濃度の場合には
膜の均一性を維持するのが困難であり、又低能度の場合
には膜の成長が阻害されるため通常最適濃度として0.
1〜10mol/Lが好ましい。When the concentration of the above solution is high, it is difficult to maintain the uniformity of the film, and when it is low, the growth of the film is hindered.
It is preferably 1 to 10 mol / L.
【0017】又、上記溶液を封入するための半透膜チュ
ーブとしては半透膜の機能を有するものであれば何れで
もよく、例えばポリビニルアルコール、セロハン等を使
用するものであり、その厚さについてもあまり厚過ぎて
は膜の成長を阻害されるため通常500μm 以下のもの
が好ましい。The semipermeable membrane tube for enclosing the solution may be any one having a semipermeable membrane function, for example, polyvinyl alcohol, cellophane, etc. may be used. If it is too thick, the growth of the film is hindered, so that the thickness is usually preferably 500 μm or less.
【0018】又、一方触媒としては通常ルイス酸を使用
するが安定性の点からFeCl3 が好ましい。この触媒
の溶液とするための溶媒としては、浸透圧との関係など
から、前記の導電性高分子モノマーの溶媒と同一の溶媒
を使用することが好ましい。On the other hand, a Lewis acid is usually used as the catalyst, but FeCl 3 is preferable from the viewpoint of stability. As the solvent for forming the catalyst solution, it is preferable to use the same solvent as the solvent for the conductive polymer monomer in view of the relationship with the osmotic pressure.
【0019】なおこの溶液の濃度についても導電性高分
子モノマーの濃度と同一の濃度にして使用することが好
ましい。The concentration of this solution is preferably the same as that of the conductive polymer monomer before use.
【0020】又、触媒溶液の温度については、導電性高
分子モノマー及び触媒の種類によって異にするものであ
るが、通常液温は−50〜150℃の範囲が好ましい。The temperature of the catalyst solution varies depending on the types of the conductive polymer monomer and the catalyst, but the liquid temperature is preferably in the range of -50 to 150 ° C.
【0021】又、触媒溶液中を走行せしめる半透膜製チ
ューブの速度は、複合膜の生成速度によって異にするも
のであるが、通常該チューブを触媒溶液中に30分〜3
時間浸漬する必要がある。その理由は触媒溶液中に浸漬
する時間が短時間であると膜が十分に成長せず、また3
時間以上浸漬しても膜の成長が顕著に表われないためで
ある。The speed of the semipermeable membrane tube which is run in the catalyst solution varies depending on the production rate of the composite membrane, but the tube is usually immersed in the catalyst solution for 30 minutes to 3 minutes.
Need to soak for hours. The reason is that if the time of immersion in the catalyst solution is short, the film does not grow sufficiently, and
This is because the growth of the film does not appear remarkably even after soaking for more than a time.
【0022】[0022]
[実施例(1)]図1に示す如く、まず触媒槽1内に2
mol/LのFeCl3 水溶液2を注入し、該水溶液の液温
を40℃に保持した。一方半透膜チューブ3としては膜
厚15μm のポリビニルアルコール膜4を使用し、これ
を180℃のチューブ成型用金型5を通して該膜4をチ
ューブ状に成型した後、該チューブ中に図2に示す如く
パイプ6を介して2mol/Lのアニリン塩酸塩水溶液7を
注入して満たした後、該チューブ3を5m/分の速度で
上記のFeCl3 水溶液2中を走行せしめつつ、該チュ
ーブ内に上記パイプ6より10mol/Lのアニリン塩酸塩
水溶液を40mol/分の滴下速度にて供給する。[Example (1)] First, as shown in FIG.
Mol / L FeCl 3 aqueous solution 2 was injected and the liquid temperature of the aqueous solution was maintained at 40 ° C. On the other hand, a polyvinyl alcohol membrane 4 having a thickness of 15 μm is used as the semipermeable membrane tube 3, and the membrane 4 is molded into a tube shape through a tube molding die 5 at 180 ° C. After injecting 2 mol / L aniline hydrochloride aqueous solution 7 through a pipe 6 to fill it as shown, the tube 3 is allowed to run in the above FeCl 3 aqueous solution 2 at a speed of 5 m / min. A 10 mol / L aniline hydrochloride aqueous solution is supplied through the pipe 6 at a dropping rate of 40 mol / min.
【0023】而して、半透膜チューブ3内にアニリン塩
酸塩水溶液7を封入した状態にてFeCl3 水溶液2内
に約2時間維持せしめてポリアニリン−ポリビニルアル
コール複合膜8を生成した後、このチューブをカッター
9にて長さ方向に切り開いてフィルム状となし、次いで
水10を満たした水洗槽11内に導入し洗浄した後、更
に乾燥室12内にて約100℃にて乾燥し、ボビン13
に巻取って本発明導電性高分子複合膜をえた。Then, the aniline hydrochloride aqueous solution 7 is enclosed in the semipermeable membrane tube 3 and kept in the FeCl 3 aqueous solution 2 for about 2 hours to form the polyaniline-polyvinyl alcohol composite film 8 and then The tube is cut open in the lengthwise direction with a cutter 9 to form a film, then introduced into a washing tank 11 filled with water 10 for washing, and then dried in a drying chamber 12 at about 100 ° C. Thirteen
The film was wound on to obtain a conductive polymer composite film of the present invention.
【0024】[実施例(2)]図1と同様の装置を使用
し、触媒槽内に2mol/LのFeCl3 のクロロフォルム
溶液を注入し、その液温を50℃に保持し、半透膜チュ
ーブとして膜厚15μm のポリビニルアルコール膜を使
用し、これを180℃のチューブ成型用金型を通してチ
ューブ状に成形した後、該チューブ中に実施例(1)と
同様にして2mol/Lの(3−オクチルチオフェン)−ク
ロロフォルム溶液を注入して満たした後、5m/分の速
度にて上記のFeCl3 のクロロフォルム溶液中を走行
せしめつつ、該チューブ内に上記管から10mol/Lの
(3−オクチルチオフェン)−クロロフォルム溶液を3
0mol/分の適正速度にて供給する。[Example (2)] Using a device similar to that shown in FIG. 1, 2 mol / L of a FeCl 3 chloroform solution was injected into the catalyst tank, and the liquid temperature was maintained at 50 ° C. to obtain a semipermeable membrane. A polyvinyl alcohol film having a film thickness of 15 μm was used as a tube, and this was molded into a tube shape through a tube-molding mold at 180 ° C., and then 2 mol / L of (3 -Octylthiophene) -chloroform solution was filled and filled with 10 mol / L of (3-octyl) from the tube while running in the FeCl 3 chloroform solution at a speed of 5 m / min. Thiophene) -chloroform solution 3
Supply at an appropriate rate of 0 mol / min.
【0025】而して半透膜チューブ内に(3−オクチル
チオフェン)−クロロフォルム溶液を封入した状態にて
FeCl3 クロロフォルム溶液内に維持せしめ、ポリ
(3−オクチルチオフェン)−ポリビニルアルコール複
合膜を生成したこのチューブをカッターにて長さ方向に
切り開いてフィルム状となし、水洗槽内に導入して5秒
間洗浄した後、更に乾燥室内に約100℃にて乾燥し、
本発明導電性高分子複合膜をえた。Then, the (3-octylthiophene) -chloroform solution was sealed in the semipermeable membrane tube and kept in the FeCl 3 chloroform solution to form a poly (3-octylthiophene) -polyvinyl alcohol composite film. This tube was cut open in the length direction with a cutter to form a film, introduced into a water washing tank and washed for 5 seconds, and further dried in a drying chamber at about 100 ° C.,
The conductive polymer composite film of the present invention was obtained.
【0026】[比較例(1)]厚さ15μm のポリエチ
レンフィルムをスプレー室内に導入し、このフィルムに
ポリピロールを吹き付けて導電性複合膜をえた。[Comparative Example (1)] A polyethylene film having a thickness of 15 μm was introduced into a spray chamber, and polypyrrole was sprayed on the film to obtain a conductive composite film.
【0027】[比較例(2)]厚さ15μm のポリエチ
レンフィルムに、1mol/Lの濃度を有する(3−オクチ
ルチオフェン)のクロロフォルム溶液をロールにて塗布
し、乾燥せしめて導電性複合膜をえた。[Comparative Example (2)] A 15 μm thick polyethylene film was coated with a chloroform solution of (3-octylthiophene) having a concentration of 1 mol / L by a roll and dried to obtain a conductive composite film. ..
【0028】斯くしてえた本発明導電性高分子複合膜と
比較例導電性複合膜について、その膜厚の均一性及び体
積固有抵抗を測定した。その結果は表1に示す通りであ
る。With respect to the conductive polymer composite film of the present invention thus obtained and the conductive composite film of the comparative example, the uniformity of the film thickness and the volume resistivity were measured. The results are shown in Table 1.
【0029】[0029]
【表1】 [Table 1]
【0030】[0030]
【発明の効果】本発明方法によれば、簡単な操作にて膜
厚が均一な導電性高分子複合膜を連続的に製造しうる等
工業上極めて有用なものである。Industrial Applicability According to the method of the present invention, a conductive polymer composite film having a uniform film thickness can be continuously produced by a simple operation, and is industrially extremely useful.
【図1】本発明方法の工程を示す説明図。FIG. 1 is an explanatory view showing steps of the method of the present invention.
【図2】本発明方法において、半透膜チューブ内に導電
性高分子モノマーを注入する工程を示す説明図。FIG. 2 is an explanatory view showing a step of injecting a conductive polymer monomer into a semipermeable membrane tube in the method of the present invention.
1…触媒槽、2…FeCl3 水溶液、3…半透膜チュー
ブ、4…ポリビニルアルコール膜、5…金型、6…パイ
プ、7…アニリン塩酸塩水溶液、8…ポリアニリン−ポ
リビニルアルコール複合膜、9…カッター、10…水、
11…水洗槽、11…乾燥室。1 ... Catalyst tank, 2 ... FeCl 3 aqueous solution, 3 ... Semipermeable membrane tube, 4 ... Polyvinyl alcohol membrane, 5 ... Mold, 6 ... Pipe, 7 ... Aniline hydrochloride aqueous solution, 8 ... Polyaniline-polyvinyl alcohol composite membrane, 9 … Cutter, 10… water,
11 ... Washing tank, 11 ... Drying room.
─────────────────────────────────────────────────────
─────────────────────────────────────────────────── ───
【手続補正書】[Procedure amendment]
【提出日】平成4年4月7日[Submission date] April 7, 1992
【手続補正1】[Procedure Amendment 1]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0025[Name of item to be corrected] 0025
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【0025】而して半透膜チューブ内に(3−オクチル
チオフェン)−クロロフォルム溶液を封入した状態にて
FeCl3 クロロフォルム溶液内に約2時間維持せし
め、ポリ(3−オクチルチオフェン)−ポリビニルアル
コール複合膜を生成したこのチューブをカッターにて長
さ方向に切り開いてフィルム状となし、水洗槽内に導入
して5秒間洗浄した後、更に乾燥室内に約100℃にて
乾燥し、本発明導電性高分子複合膜をえた。Then, the (3-octylthiophene) -chloroform solution was sealed in the semipermeable membrane tube and kept in the FeCl 3 chloroform solution for about 2 hours to obtain a poly (3-octylthiophene) -polyvinyl alcohol complex. This tube having a film formed is cut open in the lengthwise direction with a cutter to form a film, introduced into a washing tank and washed for 5 seconds, and then dried in a drying chamber at about 100 ° C. A polymer composite film was obtained.
【手続補正2】[Procedure Amendment 2]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0028[Correction target item name] 0028
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【0028】斯くしてえた本発明導電性高分子複合膜と
比較例導電性複合膜について、その膜厚の均一性及びI
2 ドープした後の体積固有抵抗を測定した。その結果は
表1に示す通りである。With respect to the conductive polymer composite film of the present invention thus obtained and the conductive composite film of the comparative example, the film thickness uniformity and I
The volume resistivity after two- doping was measured. The results are shown in Table 1.
Claims (1)
透膜製チューブを、触媒溶液中を走行せしめつつ該チュ
ーブの両面に導電性高分子膜を形成せしめた後、該チュ
ーブを長さ方向に切り開き、引続き水洗、及び乾燥を行
うことを特徴とする導電性高分子複合膜の連続製造方
法。1. A semipermeable membrane tube for enclosing a conductive polymer monomer solution is formed in such a manner that a conductive polymer membrane is formed on both surfaces of the tube while running in a catalyst solution, and then the tube is lengthwise. A continuous process for producing a conductive polymer composite film, which comprises cutting into pieces, followed by washing with water and drying.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19437091A JPH0539376A (en) | 1991-08-02 | 1991-08-02 | Continuous production of composite conductive polymer film |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19437091A JPH0539376A (en) | 1991-08-02 | 1991-08-02 | Continuous production of composite conductive polymer film |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0539376A true JPH0539376A (en) | 1993-02-19 |
Family
ID=16323465
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP19437091A Pending JPH0539376A (en) | 1991-08-02 | 1991-08-02 | Continuous production of composite conductive polymer film |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0539376A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6650010B2 (en) | 2002-02-15 | 2003-11-18 | International Business Machines Corporation | Unique feature design enabling structural integrity for advanced low K semiconductor chips |
-
1991
- 1991-08-02 JP JP19437091A patent/JPH0539376A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6650010B2 (en) | 2002-02-15 | 2003-11-18 | International Business Machines Corporation | Unique feature design enabling structural integrity for advanced low K semiconductor chips |
US6815346B2 (en) | 2002-02-15 | 2004-11-09 | International Business Machines Corporation | Unique feature design enabling structural integrity for advanced low k semiconductor chips |
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