JPS6114924B2 - - Google Patents

Info

Publication number
JPS6114924B2
JPS6114924B2 JP3628879A JP3628879A JPS6114924B2 JP S6114924 B2 JPS6114924 B2 JP S6114924B2 JP 3628879 A JP3628879 A JP 3628879A JP 3628879 A JP3628879 A JP 3628879A JP S6114924 B2 JPS6114924 B2 JP S6114924B2
Authority
JP
Japan
Prior art keywords
acetylene
gel
molded product
polymer
organic solvent
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
Application number
JP3628879A
Other languages
Japanese (ja)
Other versions
JPS55128419A (en
Inventor
Masao Kobayashi
Hideki Shirakawa
Sakuji Ikeda
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.)
Resonac Holdings Corp
Original Assignee
Showa Denko KK
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 Showa Denko KK filed Critical Showa Denko KK
Priority to JP3628879A priority Critical patent/JPS55128419A/en
Priority to PCT/JP1980/000053 priority patent/WO1980002143A1/en
Priority to GB8036773A priority patent/GB2058096B/en
Priority to DE19803041421 priority patent/DE3041421C2/en
Publication of JPS55128419A publication Critical patent/JPS55128419A/en
Priority to EP80900610A priority patent/EP0026235B1/en
Priority to US06/301,890 priority patent/US4410640A/en
Priority to US06/755,210 priority patent/US4596852A/en
Publication of JPS6114924B2 publication Critical patent/JPS6114924B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明はアセチレン高重合体の加圧成形方法に
関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for pressure molding an acetylene polymer.

遷移金属化合物と有機金属化合物から成るいわ
ゆるチーグラーナツタ触媒を用いてアセチレンを
重合して得られるアセチレン高重合体は有機半導
体として知られているが、加熱しても溶融せず、
また酸素存在下で加熱すると容易に酸化劣化を受
ける。また、このアセチレン高重合体を溶解する
溶媒も見い出されておらず、アセチレン高重合体
の実用的成形物を製造する場合には従来次の二つ
の方法のみに限られていた。
The acetylene polymer obtained by polymerizing acetylene using a so-called Ziegler-Natsuta catalyst consisting of a transition metal compound and an organometallic compound is known as an organic semiconductor, but it does not melt even when heated.
Moreover, when heated in the presence of oxygen, it easily undergoes oxidative deterioration. Furthermore, no solvent has been found that can dissolve this acetylene high polymer, and the production of practical molded products of acetylene high polymers has heretofore been limited to the following two methods.

(イ) 粉末状アセチレン高重合体を加圧成形する方
法、 (ロ) 触媒溶液と気体アセチレンの自由表面近傍の
界面および固体表面にこの触媒溶液を塗布した
表面で重合を行なつて膜状および繊維状アセチ
レン重合体を製造する方法。
(a) A method of pressure molding a powdery acetylene high polymer; (b) A method of polymerizing a catalyst solution at the interface near the free surface of gaseous acetylene and a solid surface coated with the catalyst solution to form a film-like and A method for producing a fibrous acetylene polymer.

しかしながら前者(イ)の方法では機械的強度の低
い成形品しか得られず、又後者の方法(ロ)ではフイ
ルムおよび繊維の原料が限定され、実質的には厚
みの小さい膜および繊維状の成形品しか得られな
いばかりでなく、成形品の形状も膜状および繊維
状に限定されたものであつた。
However, with the former method (a), only molded products with low mechanical strength can be obtained, and with the latter method (b), raw materials for films and fibers are limited, and in reality, thin films and fibrous molded products can be obtained. Not only could only the molded products be obtained, but the shapes of the molded products were also limited to membrane-like and fibrous-like.

本発明はかかる点に鑑みて為されたものであ
り、充分な機械的強度を持ち、かつ所定の形状の
アセチレン高重合体の成形品を成形する方法を提
供せんとするものであり、その要旨は、不活性有
機溶媒の存在下で重合して得られたアセチレン高
重合体5〜95重量%と不活性有機溶媒95〜5重量
%からなるゲル状物を、型枠の中で温度100℃以
下、圧力1.0Kg/cm2以上で加圧することを特徴と
するアセチレン高重合体の成形方法である。
The present invention has been made in view of these points, and aims to provide a method for molding an acetylene polymer molded product having sufficient mechanical strength and a predetermined shape. A gel-like material consisting of 5 to 95% by weight of an acetylene high polymer obtained by polymerization in the presence of an inert organic solvent and 95 to 5% by weight of an inert organic solvent is heated in a mold at a temperature of 100°C. The following is a method for molding an acetylene polymer, which is characterized by pressurizing at a pressure of 1.0 Kg/cm 2 or more.

不活性有機溶媒の存在下、触媒を用いてアセチ
レン高重合体と不活性有機溶媒のゲル状物を製造
する方法について次の2つの方法が挙げられる。
The following two methods are available for producing a gel of an acetylene polymer and an inert organic solvent using a catalyst in the presence of an inert organic solvent.

(1) ヘキサンを溶媒としてμ−(η:η
cyclopentadienyl)−tris(η−cyclo−
pentadinyl)dititaninm(Ti−Ti)〔(C5 H45
(C5H53Ti2〕なる特殊な遷移金属化合物の触媒
を用いてアセチレンを重合してゲル状アセチレ
ン高重合体を製造する方法)〔S.L.Hsu et.al.j.
chem.P ys.69(1),106−111(1978)〕 (2) 本発明者等の見出した(A)遷移金属化合物と(B)
有機金属化合物とからなる触媒系を用いて、重
合溶媒として芳香族化合物を用い、(A)成分の濃
度が0.1〜0.0001モル/lでアセチレンを重合
してゲル状組成物の製造方法。
(1) μ−(η 15
cyclopentadienyl)-tris(η-cyclo-
pentadinyl) dititaninm (Ti−Ti) [(C 5 H 4 ) 5
(C 5 H 5 ) 3 Ti 2 ] A method for producing a gel-like acetylene polymer by polymerizing acetylene using a special transition metal compound catalyst [SLHsu et.al.j.
chem.Pys.69(1), 106-111 (1978)] (2) (A) transition metal compound and (B) discovered by the present inventors
A method for producing a gel composition by polymerizing acetylene at a concentration of component (A) of 0.1 to 0.0001 mol/l using a catalyst system comprising an organometallic compound and an aromatic compound as a polymerization solvent.

本発明に用いられるアセチレン高重合体のゲル
状物としては上記のいずれかの方法で製造された
ものでも構わないが、(2)の方法で製造されたアセ
チレン高重合体のゲル状組成物の方が均一であ
り、その結果加圧成形して得られる成形品も均一
であるのでより望ましい。なお本発明におけるゲ
ル状物とはアセチレン高重合体が不活性有機溶媒
により膨潤した状態になつている物を意味する。
The acetylene high polymer gel composition used in the present invention may be produced by any of the above methods, but the acetylene high polymer gel composition produced by method (2) may be used. This is more desirable because it is more uniform and, as a result, the molded product obtained by pressure molding is also more uniform. In the present invention, the term gel-like material refers to a material in which an acetylene polymer is swollen with an inert organic solvent.

本発明で用いられる不活性有機溶媒としては、
脂肪族又は芳香族の炭化水素、ハロゲン化炭化水
素、エーテル、カルボン酸エステル、酸無水物、
ケトン等があげられる。
Inert organic solvents used in the present invention include:
aliphatic or aromatic hydrocarbons, halogenated hydrocarbons, ethers, carboxylic acid esters, acid anhydrides,
Examples include ketones.

これらのうちでも芳香族炭化水素及び芳香族エ
ーテルが好ましく、それらの代表例としては、ベ
ンゼン、トルエン、キシレン、エチルベンゼン、
メチルフエニルエーテル(アニソール)、エチル
フエニルエーテル、ジフエニルエーテル、n−ジ
メトキシベンゼン、p−ジメトキシベンゼン、n
−ジエトキシベンゼン、p−ジエトキシベンゼ
ン、1,3,5−トリメトキシベンゼンなどを挙
げることができる。
Among these, aromatic hydrocarbons and aromatic ethers are preferred, and representative examples thereof include benzene, toluene, xylene, ethylbenzene,
Methyl phenyl ether (anisole), ethyl phenyl ether, diphenyl ether, n-dimethoxybenzene, p-dimethoxybenzene, n
-diethoxybenzene, p-diethoxybenzene, 1,3,5-trimethoxybenzene and the like.

不活性有機溶媒は上記の1種又は2種以上の混
合溶媒でもよいし、アセチレンの重合終了後上記
の不活性有機溶媒の一部を脂肪族又は芳香族のア
ルコール、カルボン酸で置換してもよい。
The inert organic solvent may be one or a mixed solvent of two or more of the above, or a part of the above inert organic solvent may be replaced with an aliphatic or aromatic alcohol or carboxylic acid after the completion of acetylene polymerization. good.

アセチレンの重合終了後不活性有機溶媒の一部
を通常の方法により除去したり、触媒を除去する
為に有機溶媒でアセチレン重合体を洗浄すること
は一向に構わないが、加圧成形するまでアセチレ
ン高重合体を有機溶媒の存在下でゲル状物の状態
に保持しておくことが本発明の必須条件であり、
加圧成形する前にアセチレン重合体を乾燥しては
成形が不可能となる。
After the polymerization of acetylene is completed, it is perfectly acceptable to remove a part of the inert organic solvent by a conventional method or to wash the acetylene polymer with an organic solvent to remove the catalyst, but the acetylene polymer may be washed with an organic solvent to remove the catalyst. It is an essential condition of the present invention that the polymer be maintained in a gel state in the presence of an organic solvent.
If the acetylene polymer is dried before pressure molding, molding becomes impossible.

本発明で用いられるゲル状物中のアセチレン高
重合体は5〜95重量%である。ゲル状物中のアセ
チレン高重合体が5重量%未満では肉厚の均一な
成形品を製造することが困難であり、又、ゲル状
物中のアセチレン高重合体が95重量%を越えると
均一なゲル状物が得られず任意の形状の成形品を
製造することが困難となる。
The amount of acetylene high polymer in the gel material used in the present invention is 5 to 95% by weight. If the acetylene high polymer content in the gel-like material is less than 5% by weight, it is difficult to produce a molded product with uniform wall thickness, and if the acetylene high polymer content in the gel-like material exceeds 95% by weight, it will be difficult to produce a molded product with uniform wall thickness. A gel-like material cannot be obtained, making it difficult to produce molded products of arbitrary shapes.

本発明において加圧成形時の温度は100℃以
下、好ましくは80℃以下であり、100℃を越える
とアセチレン高重合体の酸化劣化が起つて不適当
である。低温で加圧成形した方がアセチレン高重
合体の酸化劣化が起らないので好ましいが、−50
℃以下での成形は実用的でない。
In the present invention, the temperature during pressure molding is 100°C or less, preferably 80°C or less; if it exceeds 100°C, oxidative deterioration of the acetylene polymer will occur, which is inappropriate. Pressure molding at low temperatures is preferable because oxidative deterioration of the acetylene polymer does not occur, but -50
Molding at temperatures below ℃ is not practical.

成形時の圧力は1Kg/cm2以上、好ましくは5
Kg/cm2であり、圧力が1Kg/cm2未満では機械的強
度の充分大きい成形品を得ることが出来ない。加
圧成形時に有機溶媒の大部分はアセチレン重合体
から除去されるが、少量の有機溶媒が残る場合も
ある。残存有機溶媒はそのままでも実用上一向差
し支えない場合もあろうが、真空乾燥等の方法で
除去してもよい。
The pressure during molding is 1Kg/ cm2 or more, preferably 5Kg/cm2 or more.
Kg/cm 2 , and if the pressure is less than 1 Kg/cm 2 , a molded product with sufficiently high mechanical strength cannot be obtained. Although most of the organic solvent is removed from the acetylene polymer during pressure molding, a small amount of organic solvent may remain. Although there may be no practical problem with the remaining organic solvent as it is, it may be removed by a method such as vacuum drying.

以上の方法により、機械的強度が強く所定の形
状の成形品を得ることができる。このようにして
得られるアセチレン高重合体の成形品の電気抵抗
は非常に低く、いわゆる半導体に特有な諸電気的
性質を示す。
By the above method, a molded product having a strong mechanical strength and a predetermined shape can be obtained. The acetylene polymer molded product thus obtained has a very low electrical resistance and exhibits various electrical properties characteristic of so-called semiconductors.

室温での比抵抗はシス構造の多いものでは108
Ω・cm程度であるが、トランス構造が多くなるに
従つて低下し、トランス構造のみのものでは104
〜103Ω・cm程度となり、また光伝導性も示す。
このアセチレン高重合体は前記の諸電気的性質を
利用することにより、たとえば電気抵抗素子、感
熱素子、感光素子などの電気機器部品を製造する
ための有機半導体材料として使用できる。
The specific resistance at room temperature is 10 8 for those with many cis structures.
It is about Ω・cm, but it decreases as the number of transformer structures increases, and for a transformer structure only, it is about 10 4
~10 3 Ω·cm, and also exhibits photoconductivity.
By utilizing the various electrical properties described above, this acetylene polymer can be used as an organic semiconductor material for manufacturing electrical equipment parts such as electrical resistance elements, heat-sensitive elements, and photo-sensitive elements.

またこの様にして得られたアセチレン高重合体
の成形品を電子受容性化合物又は電子供与性化合
物で処理することによつて電気伝導度を10-8から
103Ω-1・cm-1の広い範囲にわたつて自由に制御
することができる。
In addition, by treating the molded acetylene high polymer obtained in this way with an electron-accepting compound or an electron-donating compound, the electrical conductivity can be increased from 10 -8 to 10 -8.
It can be freely controlled over a wide range of 10 3 Ω -1 cm -1 .

これらの電子受容性化合物の代表例としては、
ヨウ素、臭素、ヨウ化臭素、五フツ化ヒ素、五フ
ツ化アンチモン、四フツ化ケイ素、五塩化リン、
五フツ化リン、塩化アルミ、臭化アルミ、パーオ
キシジスルフリルジフロライド、硫酸、硝酸、フ
ルオロ硫酸、トリフルオロメタンスルホン酸、ク
ロロ硫酸、三塩化ホウ素、三臭化ホウ素、三酸化
イオウ、二酸化窒素等をあげることができる。ま
た電子供与化合物の代表例としては、ナトリウ
ム、カリウム、セシウム等をあげることができ
る。
Representative examples of these electron-accepting compounds include:
Iodine, bromine, bromine iodide, arsenic pentafluoride, antimony pentafluoride, silicon tetrafluoride, phosphorus pentachloride,
Phosphorus pentafluoride, aluminum chloride, aluminum bromide, peroxydisulfuryl difluoride, sulfuric acid, nitric acid, fluorosulfuric acid, trifluoromethanesulfonic acid, chlorosulfuric acid, boron trichloride, boron tribromide, sulfur trioxide, nitrogen dioxide etc. can be given. Further, representative examples of electron donating compounds include sodium, potassium, cesium, and the like.

以下に実施例を挙げて本発明をさらに詳細に説
明する。
The present invention will be explained in more detail with reference to Examples below.

実施例 1 窒素ガスで完全に置換した1lのガラス製反応器
に重合溶媒として常法に従つて精製したトルエン
を200ml、触媒としてテトラブトキシチタニウム
を2.94ミリモル及びトリエチルアルミニウム7.34
ミリモルをこの順序に室温で仕込んで触媒を調製
した。触媒は均一溶液であつた。反応器を液体窒
素で冷却して系中の窒素ガスを真空ポンプで排気
した。−78℃に反応器を冷却してマグネチツク・
スターラーで触媒溶液を撹拌しながら1気圧の圧
力の精製アセチレンガスを吹き込んだ。重合反応
の初期に系全体は寒天状になり、撹拌が困難にな
つた。
Example 1 In a 1 liter glass reactor completely purged with nitrogen gas, 200 ml of toluene purified according to a conventional method was used as a polymerization solvent, 2.94 mmol of tetrabutoxytitanium and 7.34 mmol of triethylaluminum were used as catalysts.
The catalyst was prepared by charging mmol in this order at room temperature. The catalyst was a homogeneous solution. The reactor was cooled with liquid nitrogen, and the nitrogen gas in the system was exhausted using a vacuum pump. Cool the reactor to -78°C and
Purified acetylene gas at a pressure of 1 atm was blown into the catalyst solution while stirring it with a stirrer. At the beginning of the polymerization reaction, the entire system became agar-like and stirring became difficult.

アセチレンガス圧を1気圧に保つたままで24時
間重合反応をそのまま継続した。系は赤紫色を呈
した寒天状であつた。重合終了後未反応のアセチ
レンガスを除去し、系の温度を−78℃に保つたま
ま200mlの精製トルエンで4回繰り返し洗浄し
た。洗浄後も溶液はやや褐色をおび、触媒は完全
に除去されなかつた。トルエン中で膨潤したゲル
状アセチレン重合体は、フイブリルが絡み合つた
均一なチツプ状であり、粉末状や塊状のポリマー
は生成していなかつた。
The polymerization reaction was continued for 24 hours while maintaining the acetylene gas pressure at 1 atm. The system was agar-like with a reddish-purple color. After the polymerization was completed, unreacted acetylene gas was removed, and the system was washed four times with 200 ml of purified toluene while keeping the temperature at -78°C. Even after washing, the solution remained slightly brown and the catalyst was not completely removed. The gel-like acetylene polymer swollen in toluene was in the form of uniform chips with intertwined fibrils, and no powder or lump-like polymer was produced.

均一ゲル状物の一部を取り出して乾燥しゲル状
物中のアセチレン高重合体の量を測定したら、ゲ
ル状物中にアセチレン高重合体は10重量%含有さ
れていた。
When a part of the homogeneous gel was taken out and dried, and the amount of acetylene high polymer in the gel was measured, it was found that the gel contained 10% by weight of acetylene high polymer.

上記のゲル状物を内側が厚さ10mm、たて100
mm、横50mmの直方体状の型枠に入れ、クロロメツ
キしたフエロ板ではさんで、室温で100Kg/cm2
圧力でトルエンを除きながらプレス成形して膜厚
が5mmの可撓性のある強靭なフイルム状成形品を
得た。このフイルム状成形品は電気伝導度(直流
四端子法で測定)が20℃で5×10-8Ω-1・cm-1
p型半導体であつた。
The above gel-like material is 10mm thick on the inside and 100mm long.
It was placed in a rectangular parallelepiped mold with a width of 50 mm, sandwiched between chloroplated ferro plates, and press-molded at room temperature while removing toluene at a pressure of 100 Kg/cm 2 to form a flexible and strong film with a thickness of 5 mm. A film-like molded product was obtained. This film-like molded product was a p-type semiconductor with an electrical conductivity (measured by the DC four-probe method) of 5×10 -8 Ω -1 ·cm -1 at 20°C.

またこのフイルム状成形品をフラスコに入れ、
真空ポンプで空気を排気した後、ヨウ素の室温の
蒸気圧でヨウ素ガスを導入して1時間このフイル
ム状成形品を処理した。1時間処理後、未反応の
ヨウ素を真空ポンプで排気してヨウ素処理したフ
イルム状成形品を得た。こののヨウ素処理したフ
イルム状成形品は電気伝導度が20℃で95Ω-1・cm
-1のp型半導体であつた。
Also, put this film-shaped molded product into a flask,
After evacuating air with a vacuum pump, iodine gas was introduced at room temperature vapor pressure and the film-shaped molded product was treated for 1 hour. After 1 hour of treatment, unreacted iodine was evacuated using a vacuum pump to obtain an iodine-treated film-like molded product. This iodine-treated film-shaped molded product has an electrical conductivity of 95Ω -1 cm at 20℃.
-1 p-type semiconductor.

実施例 2 実施例1で重合して得られた均一ゲル状物(含
有アセチレン高重合体10重量%)を真空乾燥して
含有するアセチレン高重合体が50重量%のゲル状
物とした。
Example 2 The homogeneous gel-like material obtained by polymerization in Example 1 (containing 10% by weight of acetylene high polymer) was vacuum-dried to obtain a gel-like material containing 50% by weight of acetylene high polymer.

上記のゲル状物を内側が半径50mmの円柱状の型
枠に入れ、室温200Kg/cm2の圧力でトルエンを除
きながら成形して膜みが12mmの強靭な可撓性のあ
る円柱状の成形物を得た。この成形物は電気伝導
度が20℃で4.1×10-8Ω-1・cm-1のp型半導体であ
つた。
The above gel-like material was placed in a cylindrical mold with an inner radius of 50 mm, and molded at room temperature and under a pressure of 200 kg/cm 2 while removing toluene, a strong and flexible cylindrical mold with a film thickness of 12 mm was formed. I got something. This molded product was a p-type semiconductor with an electrical conductivity of 4.1×10 -8 Ω -1 ·cm -1 at 20°C.

この成形物をフラスコに入れ、真空ポンプで空
気を排気した後、五フツ化ヒ素の蒸気で処理し
た。得られた五フツ化ヒ素処理成形物は電気伝導
度が20℃で550Ω-1・cm-1のp型半導体であつ
た。
This molded product was placed in a flask, and after evacuating the air with a vacuum pump, it was treated with arsenic pentafluoride vapor. The resulting arsenic pentafluoride-treated molded product was a p-type semiconductor with an electrical conductivity of 550Ω -1 ·cm -1 at 20°C.

実施例 3 実施例1で重合溶媒として用いたトルエンの替
りにアニソールを用いた以外は実施例1と同様に
触媒の調製及びアセチレンの重合を行つて均一な
ゲル状物を得た。このゲル状物中のアセチレン高
重合体の含量は12重量%であつた。
Example 3 A homogeneous gel was obtained by preparing a catalyst and polymerizing acetylene in the same manner as in Example 1, except that anisole was used in place of toluene used as the polymerization solvent in Example 1. The content of acetylene high polymer in this gel was 12% by weight.

このゲル状物を真空乾燥でアセチレン高重合体
の含量を70重量%にまで濃縮し、この濃縮物を内
側が半径50mmの円柱状の型枠に入れ、室温で250
Kg/cm2の圧力でアニソールを除きながら加圧成形
して膜みが25mmの強靭な可撓性のある円柱状の成
形物を得た。この成形物は電気伝導度が20℃で
5.5×10-8Ω-1・cm-1のp型半導体であつた。
This gel-like material was vacuum-dried to concentrate the acetylene high polymer content to 70% by weight, and this concentrate was placed in a cylindrical mold with an inner radius of 50 mm and heated to 250% by weight at room temperature.
Pressure molding was performed while removing anisole at a pressure of Kg/cm 2 to obtain a tough and flexible cylindrical molded product with a film thickness of 25 mm. The electrical conductivity of this molded product is 20℃.
It was a p-type semiconductor of 5.5×10 -8 Ω -1 ·cm -1 .

この成形物をフラスコに入れ、真空ポンプで空
気を排気した後、三酸化イオウの蒸気で処理し
た。得られた三酸化イオウ処理成形物は電気伝導
度が20℃で620Ω-1・cm-1のp型半導体であつ
た。
This molded product was placed in a flask, the air was evacuated using a vacuum pump, and then treated with sulfur trioxide vapor. The obtained sulfur trioxide-treated molded product was a p-type semiconductor with an electrical conductivity of 620Ω -1 ·cm -1 at 20°C.

実施例 4 実施例1でアセチレンの重合を室温で行つた以
外は実施例1と全く同様に触媒の調製及びアセチ
レンの重合を行なつて均一なゲル状物を得た。こ
のゲル状物中のアセチレン高重合体含量は18重量
%であつた。
Example 4 A uniform gel-like material was obtained by preparing a catalyst and polymerizing acetylene in exactly the same manner as in Example 1, except that the polymerization of acetylene was carried out at room temperature. The acetylene high polymer content in this gel was 18% by weight.

このゲル状物を真空乾燥してアセチレン高重合
体の含量を40重量%にまで濃縮し、この濃縮物を
実施例3と同様な方法で加圧成形して円柱状の成
形物を得た。この成形物は電気伝導度が20℃で
2.7×10-4Ω-1・cm-1のp型半導体であつた。
This gel-like material was vacuum-dried to concentrate the acetylene high polymer content to 40% by weight, and this concentrate was pressure-molded in the same manner as in Example 3 to obtain a cylindrical molded product. The electrical conductivity of this molded product is 20℃.
It was a p-type semiconductor of 2.7×10 -4 Ω -1 ·cm -1 .

この成形物を実施例1と同様な方法でヨウ素処
理した。得られたヨウ素処理成形物は電気伝導度
が20℃で16Ω-1・cm-1のp型半導体であつた。
This molded product was treated with iodine in the same manner as in Example 1. The obtained iodine-treated molded product was a p-type semiconductor with an electrical conductivity of 16Ω -1 ·cm -1 at 20°C.

Claims (1)

【特許請求の範囲】[Claims] 1 不活性有機溶媒の存在下で重合して得られた
アセチレン高重合体5〜95重量%と不活性有機溶
媒95〜5重量%からなるゲル状物を、型枠の中で
温度100℃以下、圧力1.0Kg/cm2以上で加圧するこ
とを特徴とするアセチレン高重合体の成形方法。
1. A gel-like material consisting of 5 to 95% by weight of an acetylene high polymer obtained by polymerization in the presence of an inert organic solvent and 95 to 5% by weight of an inert organic solvent is heated in a mold at a temperature of 100°C or less. , a method for molding an acetylene polymer, characterized by pressurizing at a pressure of 1.0 Kg/cm 2 or more.
JP3628879A 1979-03-29 1979-03-29 Forming method for acetylene high polymer Granted JPS55128419A (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
JP3628879A JPS55128419A (en) 1979-03-29 1979-03-29 Forming method for acetylene high polymer
PCT/JP1980/000053 WO1980002143A1 (en) 1979-03-29 1980-03-28 Process for preparing gel-like composition of acetylene high polymer,and process for fabrication thereof
GB8036773A GB2058096B (en) 1979-03-29 1980-03-28 Process for preparing gel-like composition of acetylene high polymer and process for fabrication thereof
DE19803041421 DE3041421C2 (en) 1979-03-29 1980-03-28 Process for the production of both an easily moldable mass from an acetylene high polymer and a porous acetylene high polymer
EP80900610A EP0026235B1 (en) 1979-03-29 1980-10-23 Process for molding an acetylene high polymer and process for fabrication thereof
US06/301,890 US4410640A (en) 1979-03-29 1981-09-11 Process for producing a gel-like composition of a high polymer of acetylene, and process for molding said composition
US06/755,210 US4596852A (en) 1979-03-29 1985-07-12 Process for producing a gel-like composition of a high polymer of acetylene, and process for molding said composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3628879A JPS55128419A (en) 1979-03-29 1979-03-29 Forming method for acetylene high polymer

Publications (2)

Publication Number Publication Date
JPS55128419A JPS55128419A (en) 1980-10-04
JPS6114924B2 true JPS6114924B2 (en) 1986-04-21

Family

ID=12465595

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3628879A Granted JPS55128419A (en) 1979-03-29 1979-03-29 Forming method for acetylene high polymer

Country Status (1)

Country Link
JP (1) JPS55128419A (en)

Also Published As

Publication number Publication date
JPS55128419A (en) 1980-10-04

Similar Documents

Publication Publication Date Title
US4008203A (en) Polysulphones and method of preparation
Naarmann et al. New process for the production of metal-like, stable polyacetylene
US5151221A (en) Conductive plastic composites
US4362680A (en) Process for production of molded articles of acetylene polymer
WO1980002146A1 (en) Process for preparing highly conductive acetylene high polymer
US4596852A (en) Process for producing a gel-like composition of a high polymer of acetylene, and process for molding said composition
JPS5954014B2 (en) Method for producing acetylene high polymer molded product
US4452959A (en) Process for producing a gel-like composition of a high polymer of acetylene, and process for molding said composition
JPS6114924B2 (en)
JPS6342565B2 (en)
US4579921A (en) Process for the manufacture of polyacetylene
Sergeev et al. Oligomers and polymers with reactive acetylenic groups
KR102250299B1 (en) A process for producing polyetherketoneketone mixed resin composition and polyetherketoneketone thereof
JPS6261059B2 (en)
KR20210035161A (en) A process for producing polyetherketoneketone mixed resin composition and polyetherketoneketone thereof
JPS6160844B2 (en)
US4008205A (en) Polysulphones as insulators
JPS6120412B2 (en)
JPS6226652B2 (en)
JPH0393106A (en) Electric conductor and its manufacture
EP0442547B1 (en) Process for the preparation of intrinsically conductive shaped objects.
US4094867A (en) Manufacture of polysulphones
US5264511A (en) Polymers of bis (ethynylstyryl) benzene and related monomers
JPS6028300B2 (en) Method for producing porous acetylene polymer with fibrillar structure
JPS58127713A (en) Production of high-strength polyacetylene film