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JPH0678394B2 - Method for producing polyacetylene - Google Patents
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JPH0678394B2 - Method for producing polyacetylene - Google Patents

Method for producing polyacetylene

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Publication number
JPH0678394B2
JPH0678394B2 JP62260293A JP26029387A JPH0678394B2 JP H0678394 B2 JPH0678394 B2 JP H0678394B2 JP 62260293 A JP62260293 A JP 62260293A JP 26029387 A JP26029387 A JP 26029387A JP H0678394 B2 JPH0678394 B2 JP H0678394B2
Authority
JP
Japan
Prior art keywords
water
film
applying
acetylene
polyacetylene
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 - Fee Related
Application number
JP62260293A
Other languages
Japanese (ja)
Other versions
JPH01101314A (en
Inventor
小川  一文
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP62260293A priority Critical patent/JPH0678394B2/en
Priority to DE3886881T priority patent/DE3886881T2/en
Priority to EP88117138A priority patent/EP0312099B1/en
Publication of JPH01101314A publication Critical patent/JPH01101314A/en
Priority to US07/593,464 priority patent/US5102686A/en
Publication of JPH0678394B2 publication Critical patent/JPH0678394B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Application Of Or Painting With Fluid Materials (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Polymerisation Methods In General (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、電気材料に関するものである。更に詳しく
は、導電性や非線形光学効果を示すポリアセチレン結合
を有する有機物質に関するものである。
TECHNICAL FIELD OF THE INVENTION The present invention relates to electrical materials. More specifically, the present invention relates to an organic substance having a polyacetylene bond that exhibits conductivity and a nonlinear optical effect.

従来の技術 アセチレン誘導体のポリマは、パイ電子共役系を持つ一
次元の主鎖を分子内に保有していることで、導電性や非
線形光学効果を持つことから光、電子機能材料として広
く研究されている。
2. Description of the Related Art Polymers of acetylene derivatives have a one-dimensional main chain having a pi-electron conjugated system in the molecule, and therefore have conductivity and nonlinear optical effects, and are widely studied as optical and electronic functional materials. ing.

また、ポリアセチレンの製造方法としては、チグラーナ
ッタ触媒を用いた白川らの重合方法がよく知られてい
る。
As a method for producing polyacetylene, the polymerization method of Shirakawa et al. Using a Ziegler-Natta catalyst is well known.

一方、疎水性基と親水性基を持つ両親媒性のアセチレン
誘導体を用いれば、水面上で単分子膜を形成でき、さら
にラングミュア・ブロジェット(LB)法により累積膜を
形成することが出来ることがよく知られている。
On the other hand, if an amphipathic acetylene derivative having a hydrophobic group and a hydrophilic group is used, a monomolecular film can be formed on the water surface, and a cumulative film can be formed by the Langmuir-Blodgett (LB) method. Is well known.

LB法は、近年分子そのものに機能を持たせた分子デバイ
ス開発において、構築手段の一つとして有望視されてい
る方法である。LB法によれば、数十オングストロームオ
ーダのアセチレン誘導体の単分子膜を作成でき、さらに
その累積膜も容易に得ることが出来る。
The LB method is a promising method as a construction means in recent years in developing a molecular device in which a molecule itself has a function. According to the LB method, a monomolecular film of an acetylene derivative of the order of several tens of angstroms can be prepared, and a cumulative film thereof can be easily obtained.

発明が解決しようとする問題点 ところが、現在知られているポリアセチレン誘導体は、
酸素を含む雰囲気中では、熱や圧力あるいは紫外線など
にたいして不安定であるため、安定化させる研究が進め
られている。
Problems to be Solved by the Invention However, currently known polyacetylene derivatives are
In an atmosphere containing oxygen, it is unstable with respect to heat, pressure, ultraviolet rays, and the like, so studies for stabilizing it are underway.

しかしながら、未だにアセチレン誘導体ポリマを安定化
する方法は見いだされていない。
However, a method for stabilizing an acetylene derivative polymer has not been found yet.

問題点を解決するための手段 本発明では、有機溶媒に溶解させたアセチレン基(共役
しない独立した不飽和3重結合)を含む脂肪酸系の物質
を水面上に展開し前記有機溶媒を蒸発させた後、水面上
に残った前記アセチレン基を含む物質の分子を水面上で
水面方向にバリヤでかき集め、所定の表面圧を加えなが
ら水面上の単分子膜即ちラングミュア(L)膜の状態
で、X線、電子線またはガンマ線等の放射線を用いて重
合したり、或はアセチレン誘導体のLB膜をある一定の表
面圧の基で所定の基板上に累積した後、前述のような放
射線を用いて重合させると酸素を含む雰囲気中でも安定
なポリアセチレンが形成されることを発見した。
Means for Solving Problems In the present invention, a fatty acid-based substance containing an acetylene group (independent unsaturated triple bond that is not conjugated) dissolved in an organic solvent is spread on a water surface to evaporate the organic solvent. After that, the molecules of the substance containing the acetylene group remaining on the water surface are scraped together on the water surface in the direction of the water surface with a barrier, and a predetermined molecular pressure is applied to the monomolecular film on the water surface, that is, Langmuir (L) film. Polymerization using radiation such as rays, electron beams or gamma rays, or after accumulating LB film of acetylene derivative on a given substrate under a certain surface pressure group, polymerizing using radiation as described above. It was discovered that stable polyacetylene was formed even in an atmosphere containing oxygen.

即ち、一定の表面圧の基で圧縮しながらアセチレン誘導
体の分子を放射線重合することにより、共役系が連続し
た直鎖状で超高分子量(超共役高分子)のポリアセチレ
ンを作れることを見いだした。
That is, it was found that by radiation-polymerizing the molecule of the acetylene derivative while compressing it under a constant surface pressure group, linear polyacetylene having a continuous conjugated system and an ultrahigh molecular weight (superconjugated polymer) can be produced.

さらにまた、前記L膜を放射線重合する際や、LB膜の累
積時に面方向に直流バイアスを印加しておくと、より共
役系の長いポリアセチレンが作れることを見いだした。
Further, it was found that polyacetylene having a longer conjugated system can be produced by applying a direct-current bias in the surface direction when the L film is radiation-polymerized or when the LB film is accumulated.

作用 即ち、ある一定の表面圧の基で所定の基板上に累積した
アセチレン誘導体のLB膜や水面上に展開したアセチレン
誘導体のL膜にある一定の表面圧を加えながらX線や電
子線あるいはガンマ線などを用いて放射線重合を行うこ
とにより、重合時の分子面積の縮小を補って、共役系が
連続した直鎖状の超高分子量のポリアセチレンを作るこ
とができる。即ち、単分子状態で並んだアセチレン誘導
体分子を常に一定圧力で圧縮しておくことにより、アセ
チレン誘導体モノマの放射線重合反応が連続的に続く条
件を保つことができ、重合時の分子収縮で生じる間隙を
埋めて共役系が連続した直鎖状の超高分子量のポリアセ
チレンを作ることができる。
Action That is, X-rays, electron beams or gamma rays are applied while applying a certain surface pressure to the LB film of the acetylene derivative accumulated on the predetermined substrate or the L film of the acetylene derivative spread on the water surface under a certain constant surface pressure. By performing radiation polymerization using, for example, a linear ultra-high molecular weight polyacetylene having a continuous conjugated system can be produced by compensating for the reduction in molecular area during polymerization. That is, by constantly compressing the acetylene derivative molecules arranged in a monomolecular state at a constant pressure, it is possible to maintain the condition that the radiation polymerization reaction of the acetylene derivative monomer continuously continues, and the gap generated by the molecular contraction at the time of polymerization. Can be filled to form a linear ultrahigh molecular weight polyacetylene having a continuous conjugated system.

また、アセチレン誘導体分子を水面上で面方向にバリヤ
でかき集めたり、放射線重合を行う際、面方向に直流バ
イアスを印加しておくと、更にモノマ分子の配向性がよ
くなり、より共役系が長いポリアセチレンを作ることが
可能となる。
Further, when the acetylene derivative molecule is scraped in the plane direction on the water surface with a barrier, or when a direct current bias is applied in the plane direction during radiation polymerization, the orientation of the monomer molecule is further improved, and the conjugated system is longer. It is possible to make polyacetylene.

以下、実施例を用いて本発明の詳細を説明する。Hereinafter, the details of the present invention will be described using examples.

実施例 使用したサンプルは、数々あるが、アセチレン誘導体の
一種であるオメガトリコシノイック酸(ω−tricocynoi
c Acid(TCA);CH≡C−(CH220−COOH)の場合を用
いて説明する。
Example There are many samples used, but omega tricosinoic acid (ω-tricocynoi), which is one of the acetylene derivatives, is used.
c Acid (TCA); CH≡C- (CH 2 ) 20 -COOH) will be described.

L膜の放射線重合およびLB膜の累積には、ジヨイスレー
ベル社のトラフIV(Joice-Loebl Trough IV)を用
い、500nm以下の光をカットしたイエロー光照明のクラ
ス100のクリーンルーム内で行った。このときクリーン
ルーム内は、室温23±1℃、湿度40±5%に調節されて
いる。LB膜の累積は25層行ったが、すべてY型であっ
た。LB膜の累積に使用した基板は、直径3インチの酸化
膜を形成したSi基板である。放射線重合反応に使用した
線源はX線及び電子線である。また、水面上でのL膜及
びLB膜の重合を確認するためFTIRスペクトルを測定し
た。
The radiation polymerization of the L film and the accumulation of the LB film were carried out in a class 100 clean room of yellow light illumination in which light of 500 nm or less was cut using a trough IV (Joice-Loebl Trough IV) manufactured by JOYS LABEL. At this time, the room temperature in the clean room is adjusted to 23 ± 1 ° C and the humidity is adjusted to 40 ± 5%. The LB film was accumulated in 25 layers, but all were Y-type. The substrate used for accumulating the LB film is a Si substrate on which an oxide film having a diameter of 3 inches is formed. The radiation sources used in the radiation polymerization reaction are X-rays and electron beams. In addition, FTIR spectrum was measured to confirm the polymerization of the L film and the LB film on the water surface.

まず、分子密度あるいは分子配向性の違を確認するた
め、水相の塩濃度およびpHを変えてTCA・L膜の表面圧
分子占有面積特性(π−Aカーブ)を測定した。第1図
に代表的な2つの水槽条件でのπ−Aカーブを示す。
First, in order to confirm the difference in molecular density or molecular orientation, the surface pressure molecule occupancy area characteristic (π-A curve) of the TCA · L membrane was measured by changing the salt concentration and pH of the aqueous phase. FIG. 1 shows π-A curves under two typical water tank conditions.

次に、第1図の代表的なAおよびB点で累積したTCA・L
B膜のX線に対する反応性を調べた。A点及びB点で累
積したTCA・LB膜にそれぞれX線照射したもののエタノ
ール溶媒侵漬後の残膜率(ガンマ特性)は、第2図に示
すような変化を示し、何れも100〜200mJ/cm2で溶媒不溶
性となった。さらに化学的な解析を行うためFTIRスペク
トルを測定した。第3図、第4図はそれぞれA点とB点
で累積したTCA・LB膜のX線照射に伴うFTIRスペクトル
の変化を示す。第3および第4図に示すように、いずれ
もX線照射にともなって3300cm-1(≡CHの吸収)の吸収
が減少して、新たに1650cm-1(C=Cの吸収)の吸収が
増加していることおよびTCA・LB膜が溶媒不溶性となる
ことにより(−CH=CH−)n結合を持つポリアセチレン
が生成されたことが判る。即ち第5図(a)に示すよう
な分子配列状態からから第5図(b)に示すような反
応、即ちポリアセチレンが製造されたことが明かとなっ
た。
Next, TCA ・ L accumulated at typical points A and B in Fig. 1
The reactivity of the B film to X-ray was examined. The TCA / LB films accumulated at points A and B were irradiated with X-rays, respectively, and the residual film rate (gamma characteristic) after immersion in ethanol solvent showed the change as shown in Fig. 2, and both were 100-200 mJ / The solvent became insoluble at cm 2 . FTIR spectra were measured for further chemical analysis. 3 and 4 show changes in the FTIR spectrum of the TCA / LB film accumulated at points A and B, respectively, due to X-ray irradiation. As shown in the third and fourth figures, both reduced the absorption of 3300 cm -1 (absorption of ≡CH) with the X-ray irradiation, the absorption of new 1650 cm -1 (absorption of C = C) It can be seen that polyacetylene having (-CH = CH-) n bonds was produced due to the increase in the number and the insolubility of the TCA / LB film in the solvent. That is, it became clear that the reaction shown in FIG. 5 (b), that is, polyacetylene was produced from the molecular arrangement shown in FIG. 5 (a).

さらに第6図は、第1図のA点及びB点で累積したTCA
・LB膜のX線照射に伴う3300cm-1(≡CHの吸収)におけ
る赤外吸収強度の変化を示す。A点及びB点で累積した
ものいずれもX線照射にともなって3300cm-1の吸収が減
少しているが、B点で累積したTCA・LB膜の方が反応性
が高い。従って、TCA・LB膜を用いてポリアセチレンを
製造する場合、累積時のTCA分子の分子配向性及び分子
密度が重要なことが明かとなった。
Furthermore, Fig. 6 shows the TCA accumulated at points A and B in Fig. 1.
-The change in infrared absorption intensity at 3300 cm -1 (absorption of CH) due to X-ray irradiation of the LB film is shown. Absorption at 3300 cm -1 decreased with X-ray irradiation in both the A and B points, but the TCA / LB film accumulated at the B point had higher reactivity. Therefore, it was revealed that the molecular orientation and the molecular density of TCA molecules at the time of accumulation are important when producing polyacetylene using the TCA / LB film.

一方、第1図のA点及びB点の条件のTCA・L膜に直接
X線を100〜200mJ/cm2程度照射すると、やはり重合が進
みエタノール溶媒に不溶性となることも確認された。
On the other hand, it was also confirmed that when the TCA.L film under the conditions of points A and B in FIG. 1 was directly irradiated with X-rays at about 100 to 200 mJ / cm 2 , the polymerization also proceeded and became insoluble in the ethanol solvent.

以上の結果より、X線重合の方法では、TCA・L膜およ
びLCA・LB膜は第5図に示すような放射線重合過程を経
てポリアセチレンを生成することが確認された。
From the above results, it was confirmed that in the X-ray polymerization method, the TCA.L film and the LCA.LB film produced polyacetylene through the radiation polymerization process as shown in FIG.

一方、エネルギーが高い電子線(ガンマ線も同じ効果が
ある)を用いてTCA・L膜やTCA・LB膜に照射を行うと、
やはり同様にTCA・LB膜は溶媒不溶性となることが確認
された。
On the other hand, when the TCA / L film or TCA / LB film is irradiated with an electron beam having high energy (gamma ray has the same effect),
Similarly, it was confirmed that the TCA / LB film became solvent insoluble.

なお、この様にして製造されたポリアセチレンは、従来
触媒法で製造されていてポリアセチレン誘導体に比べ、
酸素を含む雰囲気中でも、熱や圧力あるいは紫外線など
にたいして著しく安定であった。
Incidentally, the polyacetylene produced in this manner is conventionally produced by the catalytic method, and compared with the polyacetylene derivative,
It was remarkably stable against heat, pressure, ultraviolet rays, etc. even in an atmosphere containing oxygen.

また、ジアセチレン誘導体分子を水面上で面方向にバリ
ヤでかき集めたり、放射線重合を行う際、面方向に数十
ボルトの直流バイアスを印加しておくと更にモノマ分子
の配向性がよくなり、より共役系が長いポリアセチレン
を作ることも可能なことが確認された。
In addition, when the diacetylene derivative molecules are scraped in the plane direction on the water surface with a barrier, or when radiation polymerization is performed, a direct current bias of several tens of volts is applied in the plane direction to further improve the orientation of the monomer molecules. It was confirmed that it is also possible to make polyacetylene having a long conjugated system.

以上の、実施例では、TCA・LB膜およびTCA・L膜につい
てのみ示したが、分子内にアセチレン(C≡C)基を含
みLB膜形成が可能なものであれば、累積条件は異なって
も同様の方法が利用出来ることは明らかであろう。ま
た、末端のカルボン酸の代わりに、−SiCl3のような水
に対して活性な基を付加させておけばLB膜形成法の代わ
りに化学吸着法の使用が可能なことはいうまでもない。
In the above examples, only the TCA.LB film and the TCA.L film are shown. However, if the LB film can be formed by including an acetylene (C≡C) group in the molecule, the accumulation conditions are different. It will be clear that a similar method can be used. Further, it goes without saying that the chemical adsorption method can be used instead of the LB film formation method by adding a water-active group such as --SiCl 3 instead of the terminal carboxylic acid. .

発明の効果 本発明の方法を用いることにより、導電性や非線形光学
効果の非常に優れ安定なポリアセチレンのポリマを高能
率に製造できる。なお、この方法によると、理論的には
共役系が連続して数mm或は数cm以上の長さを持つ直鎖状
の超高分子量のポリアセチレンの製造も可能であるた
め、非線形光学効果を利用したデバイスの製作には極め
て有効である。また、今後さらに原料となるジアセチレ
ン誘導体モノマの種類や製造条件を適正化することによ
り、共役系が連続して数十cm或は数m以上の長さを持つ
直鎖状で超高分子量の安定なポリアセチレンの製造も可
能になると思われるため、この方法で冷却を必要としな
い有機超電導物質の製造が可能となる。
EFFECTS OF THE INVENTION By using the method of the present invention, it is possible to highly efficiently produce a stable polyacetylene polymer having excellent conductivity and nonlinear optical effect. In addition, according to this method, it is theoretically possible to produce a linear ultrahigh molecular weight polyacetylene having a conjugated system having a length of several mm or several cm or more. It is extremely effective in manufacturing the device used. In addition, by optimizing the type and manufacturing conditions of the diacetylene derivative monomer, which will be the raw material in the future, the conjugated system will have a linear and ultra-high molecular weight with a length of several tens of centimeters or several meters or more. Since it seems that stable polyacetylene can be produced, this method enables the production of an organic superconducting material that does not require cooling.

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

第1図は代表的な2つの水槽条件におけるTCA・L膜の
π−Aカーブを示す図、第2図はX線照射に伴うTCA・L
B膜のガンマ特性図、第3図及び第4図はTCA・LB膜のX
線照射に伴うFTIRスペクトル変化を示す図、第5図はTC
A・LB膜の放射線重合過程の概念図、第6図は3300cm-1
におけるTCA・LB膜のX線照射に伴う赤外吸収強度変化
を示す図である。
Fig. 1 shows the π-A curve of TCA ・ L film under two typical water tank conditions, and Fig. 2 shows TCA ・ L accompanying X-ray irradiation.
Gamma characteristics of B film, 3 and 4 are X of TCA / LB film
Fig. 5 shows the change in FTIR spectrum due to radiation irradiation.
Conceptual diagram of radiation polymerization process of A ・ LB film, Fig. 6 is 3300cm -1
FIG. 6 is a diagram showing a change in infrared absorption intensity of the TCA / LB film in Example 1 due to X-ray irradiation.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 H01B 1/12 C 7244−5G ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification code Office reference number FI technical display location H01B 1/12 C 7244-5G

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】有機溶媒に溶解させたアセチレン(C≡
C)基を含む物質を水面上に展開し前記有機溶媒を蒸発
させた後、前記水面上に残った前記アセチレン基を含む
物質の分子を前記水面上で水面方向にバリヤでかき集
め、所定の表面圧を前記物質の分子に加えながらX線、
電子線またはガンマ線等の放射線を用いて照射して重合
させることを特徴としたポリアセチレンの製造方法。
1. An acetylene (C≡ dissolved in an organic solvent).
C) After developing a substance containing a group on the water surface and evaporating the organic solvent, molecules of the substance containing the acetylene group remaining on the water surface are scraped on the water surface in the water surface direction with a barrier, and a predetermined surface is formed. X-rays while applying pressure to the molecules of the substance,
A method for producing polyacetylene, which comprises irradiating with radiation such as electron beam or gamma ray to polymerize.
【請求項2】所定の表面圧を加えると同時に水面と平行
する方向に直流電界を印加しながら光を照射して重合さ
せることを特徴とした特許請求の範囲第1項記載のポリ
アセチレンの製造方法。
2. The method for producing polyacetylene according to claim 1, wherein the polymerization is performed by irradiating light while applying a predetermined surface pressure and at the same time applying a DC electric field in a direction parallel to the water surface. .
【請求項3】水の中に無機塩が含まれていることを特徴
とした特許請求の範囲第1項または第2項記載のポリア
セチレンの製造方法。
3. The method for producing polyacetylene according to claim 1 or 2, wherein the water contains an inorganic salt.
【請求項4】アセチレン基を含む物質がトリコシノイッ
ク酸であることを特徴とした特許請求の範囲第1項記載
のポリアセチレンの製造方法。
4. The method for producing polyacetylene according to claim 1, wherein the substance containing an acetylene group is tricosinoic acid.
【請求項5】有機溶媒に溶解させたアセチレン基を含む
物質を水面上に展開し前記有機溶媒を蒸発させた後、水
面上に残った前記アセチレン基を含む物質の分子を水面
上で水面方向にバリヤでかき集め、所定の表面圧を前記
物質の分子に加えながら所定の基板上に累積し、前記基
板上に累積されたアセチレン基を含む薄膜をX線、電子
線またはガンマ線等の放射線を用いて照射して重合させ
ることを特徴としたポリアセチレンの製造方法。
5. A substance containing an acetylene group dissolved in an organic solvent is spread on the surface of water to evaporate the organic solvent, and then the molecules of the substance containing the acetylene group remaining on the surface of the water are directed to the surface of the water. And a predetermined surface pressure is added to the molecules of the substance while accumulating on a predetermined substrate, and the thin film containing acetylene groups accumulated on the substrate is irradiated with radiation such as X-rays, electron beams or gamma rays. A method for producing polyacetylene, which comprises irradiating and polymerizing.
【請求項6】所定の表面圧を加えながら所定の基板上に
累積する工程において所定の表面圧を加えると同時に水
面と平行する方向に直流電界を印加しながら累積するこ
とを特徴とした特許請求の範囲第5項記載のポリアセチ
レンの製造方法。
6. A method of accumulating while applying a predetermined surface pressure and applying a DC electric field in a direction parallel to the water surface at the same time in the step of accumulating on a predetermined substrate while applying a predetermined surface pressure. 6. The method for producing polyacetylene according to claim 5.
【請求項7】水の中に無機塩が含まれていることを特徴
とした特許請求の範囲第5項または第6項記載のポリア
セチレンの製造方法。
7. The method for producing polyacetylene according to claim 5 or 6, wherein the water contains an inorganic salt.
【請求項8】アセチレン基を含む物質がトリコシノイッ
ク酸であることを特徴とした特許請求の範囲第5項記載
のポリアセチレンの製造方法。
8. The method for producing polyacetylene according to claim 5, wherein the substance containing an acetylene group is tricosinoic acid.
JP62260293A 1987-10-15 1987-10-15 Method for producing polyacetylene Expired - Fee Related JPH0678394B2 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP62260293A JPH0678394B2 (en) 1987-10-15 1987-10-15 Method for producing polyacetylene
DE3886881T DE3886881T2 (en) 1987-10-15 1988-10-14 Process for the production of polyacetylene.
EP88117138A EP0312099B1 (en) 1987-10-15 1988-10-14 Process for producing a polyacetylene
US07/593,464 US5102686A (en) 1987-10-15 1990-10-03 Process for producing a polyacetylene

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62260293A JPH0678394B2 (en) 1987-10-15 1987-10-15 Method for producing polyacetylene

Publications (2)

Publication Number Publication Date
JPH01101314A JPH01101314A (en) 1989-04-19
JPH0678394B2 true JPH0678394B2 (en) 1994-10-05

Family

ID=17346033

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62260293A Expired - Fee Related JPH0678394B2 (en) 1987-10-15 1987-10-15 Method for producing polyacetylene

Country Status (1)

Country Link
JP (1) JPH0678394B2 (en)

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58111029A (en) * 1981-12-24 1983-07-01 Kureha Chem Ind Co Ltd Manufacture of built-up film of diacetylene compound
JPS61134345A (en) * 1984-12-05 1986-06-21 Kanegafuchi Chem Ind Co Ltd Amphoteric diacetylene compound containing benzene ring, and membrane made thereof
JPS62260291A (en) * 1986-05-07 1987-11-12 グローリー工業株式会社 Abnormal coin processing for coin receiver
JPS63179909A (en) * 1987-01-22 1988-07-23 Agency Of Ind Science & Technol Production of polymer thin film
JPS6474205A (en) * 1987-09-14 1989-03-20 Agency Ind Science Techn Polyethynylacetylene derivative

Also Published As

Publication number Publication date
JPH01101314A (en) 1989-04-19

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