JPS5931163B2 - Method for manufacturing an organic semiconductor composed of pyrolyzed and fired carbonaceous fiber aggregate - Google Patents
Method for manufacturing an organic semiconductor composed of pyrolyzed and fired carbonaceous fiber aggregateInfo
- Publication number
- JPS5931163B2 JPS5931163B2 JP736476A JP736476A JPS5931163B2 JP S5931163 B2 JPS5931163 B2 JP S5931163B2 JP 736476 A JP736476 A JP 736476A JP 736476 A JP736476 A JP 736476A JP S5931163 B2 JPS5931163 B2 JP S5931163B2
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- Prior art keywords
- fiber aggregate
- pyrolyzed
- temperature
- carbonaceous fiber
- fired
- 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.)
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Description
【発明の詳細な説明】
本発明は繊維状有機物を熱分解温度以上に焼成して得ら
れる熱分解焼成炭素質繊維集合体より、電気抵抗値の温
度依存性が著しく小さい有機半導体の製造方法に関する
ものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing an organic semiconductor whose electrical resistance value has significantly lower temperature dependence than a pyrolyzed and fired carbonaceous fiber aggregate obtained by firing a fibrous organic substance to a temperature higher than its pyrolysis temperature. It is something.
たとえば約1000℃以上の焼成温度で生成する熱分解
焼成炭素質繊維集合体は、明確な炭素型構造を有する炭
素質繊維となるように、一般に繊維状有機物を本質的に
熱分解温度より、より高温度で焼成すると、その焼成温
度の上昇と共に焼成生成物中の炭素含有量が増加する。For example, pyrolysis-fired carbonaceous fiber aggregates produced at a firing temperature of about 1000°C or higher generally contain fibrous organic matter essentially at a temperature higher than the pyrolysis temperature so as to produce carbonaceous fibers with a distinct carbon-type structure. When firing at high temperatures, the carbon content in the fired product increases as the firing temperature increases.
いま、繊維状有機物を該繊維状有機物の熱分解温度以上
〜1000℃程度の焼成温度で熱分解焼成すると、明確
な炭素型構造を呈するには至らない(炭素含有量が十分
ではない)熱分解焼成炭素質繊維集合体、すなわち、半
導体領域の電気抵抗値を示す炭素質繊維集合体となる(
第1表参照)が、この炭素質繊維集合体は、雰囲気中の
温度が変化するに従つて前記電気抵抗値が大きく変化す
る、すなわち温度依存性が大きいことが欠点である。Now, when a fibrous organic material is pyrolyzed and fired at a calcination temperature of about 1000°C above the pyrolysis temperature of the fibrous organic material, the pyrolysis does not result in a clear carbon-type structure (the carbon content is not sufficient). It becomes a fired carbonaceous fiber aggregate, that is, a carbonaceous fiber aggregate that exhibits the electrical resistance value of the semiconductor region (
However, the disadvantage of this carbon fiber aggregate is that the electrical resistance value changes greatly as the temperature in the atmosphere changes, that is, it has a large temperature dependence.
第1表
ポリアクリルニトリル繊維先駆体を用いた熱分解焼成炭
素質繊維集合体の焼成温度と物性例えば、1.5Dのポ
リアクリルニトリル繊維3000本からなる繊維状有機
物を650〜1000℃で暁成して得られた熱分解焼成
炭素質繊維集合体について、1m当りの電気抵抗値を種
種の雰囲気温度で測定した値を、24℃の雰囲気での測
定値を基準とした電気抵抗値変化率(ξ)で表示した際
の(ξ)の変化は第1図のごとくなる。Table 1 Firing temperature and physical properties of pyrolyzed and fired carbonaceous fiber aggregates using polyacrylonitrile fiber precursors For example, a fibrous organic material consisting of 3000 1.5D polyacrylonitrile fibers is sintered at 650 to 1000°C. For the pyrolyzed and fired carbonaceous fiber aggregates obtained, the electrical resistance value per 1 m was measured at various atmospheric temperatures, and the electrical resistance value change rate ( The change in (ξ) when expressed as (ξ) is as shown in Figure 1.
第1図から明らかなように、炭素質繊維集合体の電気抵
抗値はその雰囲気温度が上昇する程減少する。そして、
前述の電気抵抗値変化率ξは、炭素質繊維集合体を得る
際の焼成温度が高くなる程小さくなり、焼成温度が10
00℃以上のものになるとその変化率ξは実用上殆ど問
題とされる程のものではなくなることが確認される。と
ころで、電気抵抗値の温度依存性が大きいということは
、例えば熱分解焼成炭素質繊維集合体を発熱体および半
導体電線として使用する場合に、その使用中に電気抵抗
値が変化することを意味し、所定の電気的特性が使用中
に失われてゆくこととなり、実用に際してはマイナスの
要因となるものであるから、或る一定の電気抵抗値を有
し、かつその電気抵抗値の温度依存性の小さい熱分解焼
成炭素質繊維集合体を得るためには、繊維集合体を構成
する単繊維の総数を減少させて該繊維集合体自体の電気
抵抗値を大きくし、その分だけ利用し得る焼成温度を高
めるようにすることが考えられる。As is clear from FIG. 1, the electrical resistance value of the carbon fiber aggregate decreases as the ambient temperature rises. and,
The above-mentioned electric resistance value change rate ξ becomes smaller as the firing temperature increases when obtaining the carbonaceous fiber aggregate, and when the firing temperature is 10
It is confirmed that when the temperature exceeds 00° C., the rate of change ξ is hardly a problem in practice. By the way, the fact that the electrical resistance value has a large temperature dependence means that, for example, when a pyrolyzed and fired carbonaceous fiber aggregate is used as a heating element or a semiconductor wire, the electrical resistance value changes during its use. , the predetermined electrical characteristics will be lost during use, which is a negative factor in practical use. In order to obtain a pyrolyzed and fired carbonaceous fiber aggregate with a small fiber aggregate, the electrical resistance value of the fiber aggregate itself is increased by reducing the total number of single fibers constituting the fiber aggregate, and the firing rate that can be utilized by that amount is increased. One possibility is to raise the temperature.
しかしながら、熱分解焼成炭素質繊維集合体を例えば半
導体電線として使用する場合には、これが半導体電線と
して実際上使用され得るに必要な強度を有していること
が不可欠な条件であるが、前述の通り繊維集合体を構成
する単繊維の総数を減少させると繊維集合体の強度が必
然的に低下することとなり、かかる面においての条件を
満足する繊維集合体を得ることが出来なくなるため、単
に焼成温度を高めることによつて電気抵抗値の温度依存
性の小さい熱分解焼成炭素質繊維集合体を得るというこ
とは因難である。However, when using a pyrolyzed and fired carbonaceous fiber aggregate as, for example, a semiconductor wire, it is an essential condition that it has the strength necessary to be practically used as a semiconductor wire. If the total number of single fibers constituting the fiber aggregate is reduced, the strength of the fiber aggregate will inevitably decrease, making it impossible to obtain a fiber aggregate that satisfies these conditions. It is difficult to obtain a pyrolyzed and fired carbonaceous fiber aggregate whose electrical resistance value has a small temperature dependence by increasing the temperature.
本発明は、繊維状有機物を該繊維状有機物の熱分解温度
以上〜1000℃程度で焼成して得られた熱分解焼成炭
素質繊維集合体を銅塩水溶液で処理し、次いで300〜
600℃にで熱処理することによる熱分解焼成炭素質繊
維集合体からなる有機半導体を得る特許請求の範囲第1
番目の発明、および繊維状有機物を該繊維状有機物の熱
分解温度以上〜1000℃程度で焼成して得られた熱分
解焼成炭素質繊維集合体を300〜600℃にて熱処理
し、次いで銅塩水溶液で処理した後、更に300〜60
0℃にて熱処理することにより熱分解焼成炭素質繊維集
合体からなる有機半導体を得る特許請求の範囲第2番目
の発明とすることにより、繊維状有機物を該有機物の熱
分解温度以上〜1000℃程度で焼成して得られた熱分
解焼成炭素質繊維集合体で、しかも電気抵抗値の温度依
存性の著しく小さい有機半導体を得るものである。In the present invention, a pyrolyzed and fired carbonaceous fiber aggregate obtained by firing a fibrous organic substance at a temperature above the thermal decomposition temperature of the fibrous organic substance to about 1000°C is treated with an aqueous copper salt solution,
Claim 1: Obtaining an organic semiconductor consisting of a pyrolyzed and fired carbonaceous fiber aggregate by heat treatment at 600°C.
In the invention, a pyrolyzed and fired carbonaceous fiber aggregate obtained by firing a fibrous organic substance at a temperature above the thermal decomposition temperature of the fibrous organic substance to about 1000°C is heat-treated at 300 to 600°C, and then a copper salt is added to the aggregate. After treatment with aqueous solution, further 300-60
According to the second aspect of the invention, an organic semiconductor consisting of a pyrolyzed and fired carbonaceous fiber aggregate is obtained by heat treatment at 0°C. The purpose of the present invention is to obtain an organic semiconductor which is a pyrolyzed and fired carbonaceous fiber aggregate obtained by firing at a certain temperature, and whose electrical resistance value has extremely low temperature dependence.
本発明において、熱分解焼成炭素質繊維集合体の先駆体
となる繊維状有機物としては、ポリアクリルニトリルな
どの合成繊維やピツチから製造される炭素質繊維など、
一般に焼成によつて炭素質繊維と総称されるものに変性
され得るものであればいかなるものでも利用できる。以
下本発明の熱分解焼成炭素質繊維集合体からなる有機半
導体の製造方法について、その具体的な構成とその効果
を実験例に基づいて説明する。In the present invention, examples of fibrous organic substances that serve as precursors of pyrolyzed and fired carbonaceous fiber aggregates include synthetic fibers such as polyacrylonitrile and carbonaceous fibers produced from pitch.
In general, any material can be used as long as it can be modified into what is generally called a carbon fiber by firing. The specific structure and effects of the method for producing an organic semiconductor made of a pyrolyzed and fired carbonaceous fiber aggregate of the present invention will be explained below based on experimental examples.
なお、本発明の熱分解焼成炭素質繊維集合体からなる有
機半導体の製造方法における銅塩水溶液処理とそれに続
く300〜600℃での熱処理とに基づく効果は、これ
らの処理に付される熱分解焼成炭素質繊維集合体を得る
際の熱分解焼成温度が1000℃程度のものまでは明確
であり、かつそのときの熱分解焼成温度が低くなる程本
各発明による前記効果が顕著となるものである。しかし
ながら、繊維状有機物を熱分解焼成して炭素質繊維集合
体を得る際の熱分解焼成温度には、熱分解焼成を効率良
く実施するため、或る一定の温度以上で熱分解焼成する
ことが常識であり、因みに、ポリアクリルニトリル繊維
を効率良く熱分解し得る代表的な最低温度は約700℃
程度とされているので、炭素質繊維集合体を本発明の処
理に付すに当たつて利用する炭素質繊維集合体として、
熱分解焼成温度720℃〜850℃を利用して焼成した
ポリアクリルニトリル繊維からの炭素質繊維集合体を使
用する場合に基づいて、以下の具体例を説明する。実験
例 1
1.5D×6000本のポリアクリルニトリル繊維を空
気の存在下で27『C・3時間焼成したあとさらに窒素
雰囲気下で720℃・7分間焼成して得られた熱分解焼
成炭素質繊維集合体(以下CF6OOO集合体と略称す
る)を、各種の金属塩水溶液に浸漬し、180℃で乾燥
させ、次いで4500C・7分間の熱処理を行つた。Note that the effects based on the copper salt aqueous solution treatment and the subsequent heat treatment at 300 to 600°C in the method for producing an organic semiconductor comprising a pyrolyzed and fired carbonaceous fiber aggregate of the present invention are due to the pyrolysis caused by these treatments. It is clear that the pyrolysis and sintering temperature used to obtain the sintered carbonaceous fiber aggregate is up to about 1000°C, and the lower the pyrolysis and sintering temperature is, the more remarkable the effects of the present invention become. be. However, in order to efficiently carry out pyrolysis and sintering when pyrolyzing and sintering fibrous organic matter to obtain a carbonaceous fiber aggregate, pyrolysis and sintering must be carried out at a certain temperature or higher. This is common sense, and by the way, the typical minimum temperature at which polyacrylonitrile fiber can be thermally decomposed efficiently is approximately 700°C.
Therefore, as a carbonaceous fiber aggregate to be used when subjecting the carbonaceous fiber aggregate to the treatment of the present invention,
The following specific example will be explained based on the case of using a carbonaceous fiber aggregate made from polyacrylonitrile fibers fired using a pyrolysis firing temperature of 720°C to 850°C. Experimental Example 1 Pyrolytic calcined carbonaceous material obtained by firing 1.5D x 6000 polyacrylonitrile fibers at 27°C for 3 hours in the presence of air and then firing them at 720℃ for 7 minutes in a nitrogen atmosphere. The fiber aggregate (hereinafter abbreviated as CF6OOO aggregate) was immersed in various metal salt aqueous solutions, dried at 180°C, and then heat-treated at 4500C for 7 minutes.
上記の金属塩水溶液処理を行つたCF6OOO集合体を
長さ1mに切断したものの電気抵抗値の雰囲気温度を変
えて測定した値を24℃における電気抵抗値を基準とし
てその変化率ξで表示し、第2−1図に示した。The electrical resistance value of the CF6OOO aggregate treated with the above metal salt aqueous solution is cut into 1 m length, and the value measured by changing the ambient temperature is expressed as the rate of change ξ based on the electrical resistance value at 24 ° C. It is shown in Figure 2-1.
図より明らかなように、銅塩(CuCl2)水溶液によ
る処理系の電気抵抗値の温度依存性は著しく小さく、ア
ルミニウム塩、リチウム塩あるいはマグネシウム塩のご
とき塩類水溶液による処理は、その効果がほとんど表わ
れていない。As is clear from the figure, the temperature dependence of the electrical resistance value of the system treated with a copper salt (CuCl2) aqueous solution is extremely small, and the effect is hardly visible when treated with aqueous salt solutions such as aluminum salts, lithium salts, or magnesium salts. Not yet.
なお、参考までに、この銅塩水溶液に浸漬したのち、1
80℃で乾燥させ、次の熱処理を省略したものの電気抵
抗値変化率ξは、であり、この変化率は無処理のものの
変化率と本質的に同じものであり、銅塩水溶液の浸漬処
理後の300〜600℃程度好ましくは400〜500
℃程度の熱処理は不可欠のものであることが判る。For reference, after immersing in this copper salt aqueous solution, 1
The rate of change in electrical resistance value ξ of the sample dried at 80°C and omitted the next heat treatment is ξ, and this rate of change is essentially the same as the rate of change of the sample without treatment, and after the immersion treatment in a copper salt aqueous solution. about 300 to 600℃, preferably 400 to 500℃
It can be seen that heat treatment at a temperature of about °C is essential.
実験例 2
1.5D×3000本のポリアクリルニトリル繊維を空
気の存在下で270℃・3時間焼成し、さらに窒素雰囲
気下で75『C・7分間焼成して得られた熱分解焼成炭
素質繊維集合体を種々の銅塩水溶液に浸漬し、次いで4
5『C・7分間の熱処理を行つた。Experimental Example 2 Pyrolytic calcined carbonaceous material obtained by firing 1.5D x 3000 polyacrylonitrile fibers at 270°C for 3 hours in the presence of air, and then firing at 75°C for 7 minutes in a nitrogen atmosphere. The fiber aggregate was immersed in various copper salt aqueous solutions, and then 4
5. Heat treatment was performed for 7 minutes at C.
上記の金属塩処理系を長さ1mに切断したものの電気抵
抗値変化率ξを第2−2図に示した。Figure 2-2 shows the electrical resistance change rate ξ of the metal salt treated system cut into 1 m length.
図より、銅塩としてCUCl2水溶液を使用したものの
電気抵抗値の温度依存性が著しく小さいことが明らかで
あり、CUCl2水溶液による銅塩水溶液のほかに、ア
ニオンがBr−やF一等で形成されている銅塩水溶液で
も、ほ〜同様の効果を奏することが確認されている。実
験例 3
CF6000集合体を第1工程として先ず熱処理を行い
、次いで第2工程として銅塩水溶液による浸漬処理をし
、最終工程として450℃・10分間の熱処理を行つた
のちに、長さ1mに切断したものの電気抵抗値変化率ξ
を第3図に示した。From the figure, it is clear that the temperature dependence of the electrical resistance value is extremely small when a CUCl2 aqueous solution is used as the copper salt. It has been confirmed that an aqueous copper salt solution has similar effects. Experimental Example 3 The CF6000 aggregate was first heat treated as the first step, then immersed in a copper salt aqueous solution as the second step, and heat treated at 450°C for 10 minutes as the final step, after which it was cut into a length of 1 m. Electrical resistance change rate ξ of the cut object
is shown in Figure 3.
図より、CUCl2水溶液の溶液濃度が高い程、即ちC
UCl2の付着量が多い程電気抵抗値の温度依存性は小
さくなり、また、銅塩水溶液による浸漬処理に先だつて
熱処理を施したものの電気抵抗値の温度依存性は熱処理
を行わないものに比較して若干小さくなることが明瞭で
あり、銅塩水溶液による浸漬処理を省略して、熱処理の
みを行つたもの、あるいは第1熱処理および第2熱処理
のみを行つたものは、銅塩水溶液による浸漬処理に次い
で熱処理を行つたものと比較して、そのものの電気抵抗
値の温度依存性は明らかに大きく、銅塩水溶液による浸
漬処理と、その後の熱処理工程が不可欠な工程であるこ
とが確認できる。この場合、銅塩水溶液による浸漬処理
に次いで行われる熱処理は、繊維表面が全く変化を受け
ない程度の低温度熱処理ではその効果が発揮されず、繊
維表面がエツチングされる程度の温度で熱処理されなけ
ればならなく、一般に300〜600℃程度、好ましく
は400〜500℃程度で1〜60分間、好ましくは2
〜25分程度の熱処理が必要である。実験例 41.5
D×3000本のポリアクリルニトリル繊維を空気の存
在下で270゜C・3時間焼成し、さらに窒素雰囲気下
で75『C・7分間焼成した熱分解焼成炭素質繊維集合
体(以下CF3OOO−A集合体と略称する)および1
.5D×3000本のポリアクリ々ニトリル繊維を空気
の存在下で270アC・3時間焼成し、さらに窒素雰囲
気下で850℃・7分間焼成した熱分解焼成炭素質繊維
集合体(以下CF3OOO−B集合体と略称する)をそ
れぞれ第1工程として熱処理したあと、第2工程として
銅塩水溶液による浸漬処理を行い、第3工程として45
0℃・7分間の熱処理を行つた。From the figure, the higher the solution concentration of the CUCl2 aqueous solution, the higher the C
The greater the amount of UCl2 deposited, the smaller the temperature dependence of the electrical resistance value, and the temperature dependence of the electrical resistance value of samples that were heat-treated prior to immersion in a copper salt aqueous solution was greater than that of samples that were not heat-treated. It is clear that the size becomes slightly smaller due to the copper salt aqueous solution immersion treatment. The temperature dependence of the electrical resistance value of this material was clearly greater than that of the material that was then subjected to heat treatment, confirming that the immersion treatment in a copper salt aqueous solution and the subsequent heat treatment step are essential steps. In this case, the heat treatment that follows the immersion treatment with a copper salt aqueous solution will not be effective if the heat treatment is performed at a low temperature that does not cause any change to the fiber surface; it must be heat treated at a temperature that etches the fiber surface. Generally, the temperature is about 300 to 600°C, preferably about 400 to 500°C, for 1 to 60 minutes, preferably 2 minutes.
A heat treatment of about 25 minutes is required. Experimental example 41.5
D x 3000 polyacrylonitrile fibers were fired at 270°C for 3 hours in the presence of air, and then fired at 75°C for 7 minutes in a nitrogen atmosphere to produce a pyrolyzed and fired carbonaceous fiber aggregate (hereinafter referred to as CF3OOO-A). abbreviated as aggregate) and 1
.. 5D x 3000 polyacrylic nitrile fibers were fired at 270℃ for 3 hours in the presence of air, and then fired at 850℃ for 7 minutes in a nitrogen atmosphere to create a pyrolyzed carbonaceous fiber aggregate (hereinafter referred to as CF3OOO-B aggregate). After the first step is heat treatment for each of the 45 mm (45 mm)
Heat treatment was performed at 0°C for 7 minutes.
これらの金属塩処理系を長さ1mに切断したものの電気
抵抗値変化率ξを第4図に示した。図より、CF3OO
O−A集合体やCF3OOO−B集合体の場合も、前述
のCF6OOO集合体の場合と同様に、熱処理一銅塩水
溶液による浸漬処理一熱処理の3工程を熱分解焼成炭素
質繊維集合体に施した場合には、電気抵抗値の温度依存
性が小さいものに改質されることが明瞭である。また、
熱分解焼成炭素質繊維集合体を得る際の熱分解焼成温度
が一定のものの場合、これを電気抵抗値の温度依存性の
小さいものに改質するには、熱処理の繰り返しだけでは
不十分であり、銅塩水溶液による浸漬処理が不可欠であ
ることが分る。上記実験例3より明らかなように、一般
に熱分解焼成炭素質繊維集合体に銅塩水溶液による浸漬
処理を施すに先だつて熱分解焼成炭素質繊維集合体を一
度熱処理したものの電気抵抗値の温度依存性は、この熱
処理を行わないものに比較して若干小さくなり、本発明
の目的とする効果が一層奏されるものとなる。しかしな
がら、この程度の効果の相違は、例えば銅塩水溶液によ
る浸漬処理時の銅塩水溶液の濃度を高めたり、あるいは
銅塩水溶液処理後に行う熱処理温度を高くしたりするな
どすれば、銅塩水溶液による処理に先だつた熱処理を行
わなくても十分に奏される効果であるので、いづれの工
程を採用するかは工程上における経済性を考慮して選択
されるところである。FIG. 4 shows the rate of change in electrical resistance value ξ of these metal salt treated systems cut into lengths of 1 m. From the figure, CF3OO
In the case of O-A aggregates and CF3OOO-B aggregates, as in the case of the CF6OOO aggregates described above, the pyrolyzed and fired carbonaceous fiber aggregates are subjected to the three steps of immersion in a heat-treated copper salt aqueous solution and heat treatment. In this case, it is clear that the electrical resistance value is modified to have a small temperature dependence. Also,
If the pyrolysis and sintering temperature is constant when obtaining a pyrolyzed and sintered carbonaceous fiber aggregate, repeated heat treatments alone are not sufficient to modify the pyrolysis and sintering temperature into one with a small temperature dependence of electrical resistance. It turns out that immersion treatment with a copper salt aqueous solution is essential. As is clear from Experimental Example 3 above, in general, the temperature dependence of the electrical resistance value of the pyrolyzed and sintered carbonaceous fiber aggregate is heat-treated before the pyrolyzed and sintered carbonaceous fiber aggregate is immersed in a copper salt aqueous solution. The heat treatment is slightly smaller than that of a material not subjected to this heat treatment, and the desired effects of the present invention are further exhibited. However, this level of difference in effectiveness can be reduced by increasing the concentration of the copper salt aqueous solution during the immersion treatment with the copper salt aqueous solution, or by increasing the heat treatment temperature after the copper salt aqueous solution treatment. Since this effect can be sufficiently achieved without heat treatment prior to the treatment, the choice of which process to adopt should be made in consideration of the economic efficiency of the process.
第1図はポリアクリルニトリノ橿維からなる繊維状有機
物を650〜1000℃で暁成して得られた熱分解焼成
炭素質繊維集合体の電気抵抗値変化率の温度依存性をグ
ラフで表示したもの、第2−1および第2−2図はポリ
アクリルニトリル繊維を熱分解後、金属塩の種類を変え
て金属塩処理したものの電気抵抗値変化率の温度依存性
をグラフで表示したもの、第3図および第4図はポリア
クリルニトリル繊維を熱分解後、CUCl2水溶液の濃
度を変えて処理したものの電気抵抗値変化率の温度依存
性をグラフで表示したものである。Figure 1 is a graph showing the temperature dependence of the electrical resistance change rate of a pyrolyzed and fired carbon fiber aggregate obtained by forming a fibrous organic material consisting of polyacrylonitrino fibers at 650 to 1000°C. Figures 2-1 and 2-2 are graphical representations of the temperature dependence of the rate of change in electrical resistance of polyacrylonitrile fibers treated with different metal salts after thermal decomposition. , 3 and 4 are graphical representations of the temperature dependence of the rate of change in electrical resistance of polyacrylonitrile fibers treated with varying concentrations of CUCl2 aqueous solution after thermal decomposition.
Claims (1)
1000℃程度で焼成して得られた熱分解焼成炭素質繊
維集合体を銅塩水溶液で処理し、次いで300〜600
℃にて熱処理することを特徴とする熱分解焼成炭素質繊
維集合体からなる有機半導体の製造方法。 2 繊維状有機物を該繊維状有機物の熱分解温度以上〜
1000℃程度で焼成して得られた熱分解焼成炭素質繊
維集合体を300〜600℃にて熱処理し、次いで銅塩
水溶液で処理した後、更に300〜600℃にて熱処理
することを特徴とする熱分解焼成炭素質繊維集合体から
なる有機半導体の製造方法。[Scope of Claims] 1. Fibrous organic matter is heated to a temperature higher than the thermal decomposition temperature of the fibrous organic matter.
The pyrolyzed and fired carbonaceous fiber aggregate obtained by firing at about 1000°C is treated with a copper salt aqueous solution, and then heated to 300 to 600°C.
A method for producing an organic semiconductor comprising a pyrolyzed and fired carbonaceous fiber aggregate, characterized by heat treatment at ℃. 2 The fibrous organic material is heated to a temperature higher than the thermal decomposition temperature of the fibrous organic material.
The pyrolyzed and fired carbonaceous fiber aggregate obtained by firing at about 1000°C is heat-treated at 300-600°C, then treated with an aqueous copper salt solution, and then further heat-treated at 300-600°C. A method for producing an organic semiconductor comprising a pyrolyzed and fired carbonaceous fiber aggregate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP736476A JPS5931163B2 (en) | 1976-01-26 | 1976-01-26 | Method for manufacturing an organic semiconductor composed of pyrolyzed and fired carbonaceous fiber aggregate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP736476A JPS5931163B2 (en) | 1976-01-26 | 1976-01-26 | Method for manufacturing an organic semiconductor composed of pyrolyzed and fired carbonaceous fiber aggregate |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5291194A JPS5291194A (en) | 1977-08-01 |
| JPS5931163B2 true JPS5931163B2 (en) | 1984-07-31 |
Family
ID=11663902
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP736476A Expired JPS5931163B2 (en) | 1976-01-26 | 1976-01-26 | Method for manufacturing an organic semiconductor composed of pyrolyzed and fired carbonaceous fiber aggregate |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5931163B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62290079A (en) * | 1986-06-10 | 1987-12-16 | オムロン株式会社 | Terminal block for electric equipment |
-
1976
- 1976-01-26 JP JP736476A patent/JPS5931163B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62290079A (en) * | 1986-06-10 | 1987-12-16 | オムロン株式会社 | Terminal block for electric equipment |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5291194A (en) | 1977-08-01 |
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