JPS6250574B2 - - Google Patents
Info
- Publication number
- JPS6250574B2 JPS6250574B2 JP3824883A JP3824883A JPS6250574B2 JP S6250574 B2 JPS6250574 B2 JP S6250574B2 JP 3824883 A JP3824883 A JP 3824883A JP 3824883 A JP3824883 A JP 3824883A JP S6250574 B2 JPS6250574 B2 JP S6250574B2
- Authority
- JP
- Japan
- Prior art keywords
- volume
- hydrogen chloride
- atmosphere
- oxygen
- fiber
- 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
Links
- 229920000049 Carbon (fiber) Polymers 0.000 claims description 20
- 239000004917 carbon fiber Substances 0.000 claims description 20
- 239000012298 atmosphere Substances 0.000 claims description 18
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 16
- 229910000041 hydrogen chloride Inorganic materials 0.000 claims description 15
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 claims description 15
- 239000000835 fiber Substances 0.000 claims description 14
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 11
- 239000001301 oxygen Substances 0.000 claims description 11
- 229910052760 oxygen Inorganic materials 0.000 claims description 11
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 10
- 239000011261 inert gas Substances 0.000 claims description 8
- 229920002239 polyacrylonitrile Polymers 0.000 claims description 8
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 230000001590 oxidative effect Effects 0.000 claims description 4
- 238000003763 carbonization Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 238000004513 sizing Methods 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 5
- 238000007796 conventional method Methods 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- BAPJBEWLBFYGME-UHFFFAOYSA-N Methyl acrylate Chemical compound COC(=O)C=C BAPJBEWLBFYGME-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229910052736 halogen Inorganic materials 0.000 description 2
- 150000002367 halogens Chemical class 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 1
- JAHNSTQSQJOJLO-UHFFFAOYSA-N 2-(3-fluorophenyl)-1h-imidazole Chemical compound FC1=CC=CC(C=2NC=CN=2)=C1 JAHNSTQSQJOJLO-UHFFFAOYSA-N 0.000 description 1
- OEPOKWHJYJXUGD-UHFFFAOYSA-N 2-(3-phenylmethoxyphenyl)-1,3-thiazole-4-carbaldehyde Chemical compound O=CC1=CSC(C=2C=C(OCC=3C=CC=CC=3)C=CC=2)=N1 OEPOKWHJYJXUGD-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 description 1
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 1
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 1
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 1
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000000578 dry spinning Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- FQPSGWSUVKBHSU-UHFFFAOYSA-N methacrylamide Chemical compound CC(=C)C(N)=O FQPSGWSUVKBHSU-UHFFFAOYSA-N 0.000 description 1
- LVHBHZANLOWSRM-UHFFFAOYSA-N methylenebutanedioic acid Natural products OC(=O)CC(=C)C(O)=O LVHBHZANLOWSRM-UHFFFAOYSA-N 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000009987 spinning Methods 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Description
本発明は取り扱い容易な高強度炭素繊維の製造
方法に関する。
高強度の炭素繊維を得るための炭化処理工程の
雰囲気として従来から、例えば特公昭44−21175
号公報に記載ごとく真空中または水素のような非
酸化性雰囲気、特公昭44−24692号公報に記載の
ごとく塩酸ガスなどの酸蒸気の雰囲気或いは特公
昭47−40575号公報に記載のごとくハロゲン化水
素雰囲気ならびに特公昭53−19047号公報に記載
のごとく塩化水素−水−不活性ガス雰囲気中でそ
れぞれ行なうことが知られている。
しかしながら、これらの雰囲気中で炭化して得
た炭素繊維はいずれも製造工程中の取り扱いに問
題があり、「ケバ」すなわち「単糸切れ」が発生
し易いという欠点を有していた。このため、合成
樹脂などを少量表面に塗布してサイジングするこ
とが行なわれるが、通常このサイジングする樹脂
の種類、量などを炭素繊維の取り扱い条件に合わ
せ適宜調節する必要があることから、サイジング
することなしに取り扱い易い炭素繊維の出現が望
まれてきた。
本発明の目的は前記従来技術の欠点を解消した
取り扱い易く、かつ高強度を有する炭素繊維を製
造する方法を提供するものであつて、その要旨と
するところはポリアクリロニトリル系繊維を酸化
性雰囲気中で加熱して耐炎化したのち、塩化水素
0.2〜10容量%、酸素0.2〜4容量%および不活性
ガスを含有する雰囲気中で加熱することを特徴と
する炭素繊維の製造方法にある。以下、本発明を
具体的に詳述する。
本発明において使用するポリアクリロニトリル
系繊維(以下、PAN繊維という)はポリアクリ
ロニトリル単独重合体または85重量%以上のポリ
アクリロニトリルとエチレン系不飽和化合物、例
えばアクリル酸メチル、メタクリル酸メチルまた
は酢酸ビニルのようなエステル類、塩化ビニル、
塩化ビニリデンのようなハロゲン類、アクリル
酸、メタクリル酸、イタコン酸などの酸類、アク
リルアマイド、メタクリルアマイドなどのアマイ
ド類などとの共重合体、混合体などを使用するこ
とができ、これらは湿式、乾式のいずれの紡糸法
によつても紡糸が可能であり、また溶媒としては
ロダン酸塩、硝酸、ジメチルホルムアミド、ジメ
チルアセトアミド、ジメチルスルホキシドを用い
ることができる。
繊維束としては単繊維度0.1〜10デニール パ
ー フイラメント(dpf)のフイラメントで数十
〜数十万本構成の繊維束が通常用いられるが、好
ましくは1〜5dpfのフイラメントが望ましい。
このPAN繊維を300℃以下、好ましくは230〜
280℃で酸素、ハロゲンガス、空気等の酸化性雰
囲気にて0.5〜3時間加熱して耐炎化する。この
際、原繊維長に対し数%以下の収縮または若干の
伸長を与える程度に張力を付与することが好まし
い。
次に耐炎化繊維は塩化水素0.5〜10容量%、酸
素0.2〜4容量%およびチツ素、アルゴンなどの
不活性ガスを含有する雰囲気中で300〜1500℃ま
で加熱する。このようにして得た炭素繊維はさら
に必要に応じ2000〜3000℃まで熱処理して黒鉛繊
維とすることもできる。
本発明において塩化水素、酸素の割合を前記の
ごとく限定した理由は次の通りである。
塩化水素−酸素−不活性ガス雰囲気において、
塩化水素を0.2容量%未満、酸素0.2容量%未満で
は「単糸切れ」の発生を防止する効果は認められ
ず、塩化水素10容量%、酸素4容量%を越えると
「単糸切れ」の発生が増加し、かつ強度も低下し
てくる。従つて、炭素化においては、塩化水素の
含有量0.2〜10容量%、酸素の含有量0.2〜4容量
%、好ましくは0.3〜3容量%および不活性ガス
を含有する雰囲気中で加熱することが望ましい。
従来の方法によると、塩化水素の存在は炭化時
間の短縮、強度の向上の面において効果があると
され、その量は雰囲気中10容量%以上が好適とさ
れてきた。しかし、多量の塩化水素の存在は排気
ガスの処理の面において困難な問題をかかえてお
り、また特公昭53−19047号に記載のごとく塩化
水素量を0.3〜30容量%におさえるかわりに水0.5
〜6容量%を加える方法も熱処理装置の腐食の面
において問題をかかえていた。
さらに、従来の方法で得た炭素繊維の大きな問
題はボビンに巻きうつしたりボビンから取り出し
たり、プラスチツク等と複合するため引き揃えた
り、製織したりするに際、繊維束を構成する単繊
維が切れて(「単糸切れ」)、からまるなどのトラ
ブルが発生し易いことであつた。従来の方法で得
た炭素繊維はサイジングによつても「単糸切れ」
を防止することはできなかつた。
本発明の方法によると、塩化水素の量を低くお
さえることができるため排気ガスの処理がきわめ
て容易であり、かつ水分が存在しないため装置の
腐食の問題も少ない。さらに塩化水素と酸素との
組み合わせによる雰囲気下での炭化は、得られる
炭素繊維の「単糸切れ」の発生を著しく低減させ
る効果を有する。
従つて、本発明により得られた高強度炭素繊維
は苛酷な取り扱い条件下でもサイジングなしで、
あるいは特別なサイジングを施すことなく充分使
用することができる。
以下、本発明を実施例および比較例に基づいて
具体的に説明する。
実施例1〜12および比較例1〜13
アクリロニトリル含有量95%、9000デニール、
6000フイラメントのPAN繊維を空気中で0.1g/
d張力下250℃で1時間加熱して耐炎化したの
ち、第1表に示すHCl−O2−N2雰囲気中の種々
の塩化水素濃度、酸素濃度で1400℃まで加熱炭化
した。炭化に要した時間は2分間であつた。得ら
れた炭素繊維の特性を第1表に示した。なお「単
糸切れ」の発生数は第1図に示すようにボビン1
から引き出し炭素繊維束2をボビン1の中心から
L=50cm離れたガイドロール3に導き、ボビン1
に固定して錘4により500gの荷重をかけ次いで
炭素繊維束2の中央部にm=10cmのところからブ
ロア5により20m/secの気流(室温)を30秒間
吹き付けたのち「単糸切れ」の発生数を測定し
た。
The present invention relates to a method for producing high-strength carbon fibers that are easy to handle. Traditionally, as an atmosphere for the carbonization process to obtain high-strength carbon fibers, for example,
In a vacuum or a non-oxidizing atmosphere such as hydrogen as described in Japanese Patent Publication No. 44-24692, in an atmosphere of acid vapor such as hydrochloric acid gas as described in Japanese Patent Publication No. 44-24692, or in a halogenated atmosphere as described in Japanese Patent Publication No. 47-40575. It is known to carry out the reaction in a hydrogen atmosphere and in a hydrogen chloride-water-inert gas atmosphere as described in Japanese Patent Publication No. 53-19047. However, carbon fibers obtained by carbonization in these atmospheres all have problems in handling during the manufacturing process, and have the disadvantage of being prone to "fluff" or "single yarn breakage." For this reason, sizing is carried out by applying a small amount of synthetic resin to the surface, but usually the type and amount of resin used for sizing must be adjusted appropriately according to the handling conditions of the carbon fiber, so sizing is carried out. The appearance of carbon fiber that is easy to handle has been desired. An object of the present invention is to provide a method for producing carbon fibers that are easy to handle and have high strength, eliminating the drawbacks of the prior art. After heating with hydrogen chloride to make it flame resistant,
A method for producing carbon fibers, characterized by heating in an atmosphere containing 0.2 to 10% by volume, 0.2 to 4% by volume of oxygen, and an inert gas. Hereinafter, the present invention will be specifically explained in detail. The polyacrylonitrile fiber (hereinafter referred to as PAN fiber) used in the present invention is a polyacrylonitrile homopolymer or a combination of polyacrylonitrile of 85% by weight or more and an ethylenically unsaturated compound, such as methyl acrylate, methyl methacrylate, or vinyl acetate. esters, vinyl chloride,
Copolymers and mixtures with halogens such as vinylidene chloride, acids such as acrylic acid, methacrylic acid, and itaconic acid, and amides such as acrylamide and methacrylamide can be used. Spinning can be performed by any dry spinning method, and rhodanate, nitric acid, dimethylformamide, dimethylacetamide, and dimethylsulfoxide can be used as the solvent. As the fiber bundle, a fiber bundle consisting of tens to hundreds of thousands of filaments with a single fiber density of 0.1 to 10 denier per filament (dpf) is usually used, but filaments of 1 to 5 dpf are preferably used. This PAN fiber is heated to 300℃ or less, preferably 230℃ or less.
Heat at 280°C in an oxidizing atmosphere such as oxygen, halogen gas, air, etc. for 0.5 to 3 hours to make it flame resistant. At this time, it is preferable to apply tension to an extent that causes contraction of several percent or less or slight elongation with respect to the fibril length. The flame-resistant fibers are then heated to 300-1500° C. in an atmosphere containing 0.5-10% by volume of hydrogen chloride, 0.2-4% by volume of oxygen, and an inert gas such as nitrogen or argon. The carbon fiber thus obtained can be further heat-treated to 2,000 to 3,000°C to form graphite fiber, if necessary. The reason why the proportions of hydrogen chloride and oxygen are limited as described above in the present invention is as follows. In a hydrogen chloride-oxygen-inert gas atmosphere,
If hydrogen chloride is less than 0.2% by volume and oxygen is less than 0.2% by volume, no effect on preventing "single thread breakage" is observed, and if hydrogen chloride exceeds 10% by volume and oxygen is 4% by volume, "single thread breakage" occurs. increases, and the strength also decreases. Therefore, in carbonization, heating may be performed in an atmosphere containing hydrogen chloride content of 0.2 to 10% by volume, oxygen content of 0.2 to 4% by volume, preferably 0.3 to 3% by volume, and an inert gas. desirable. According to conventional methods, the presence of hydrogen chloride is said to be effective in shortening carbonization time and improving strength, and the amount of hydrogen chloride in the atmosphere has been considered to be preferably 10% by volume or more. However, the presence of a large amount of hydrogen chloride poses a difficult problem in the treatment of exhaust gas, and as described in Japanese Patent Publication No. 53-19047, instead of suppressing the amount of hydrogen chloride to 0.3 to 30% by volume, water 0.5
The method of adding ~6% by volume also had problems in terms of corrosion of the heat treatment equipment. Furthermore, a major problem with carbon fibers obtained using conventional methods is that the single fibers that make up the fiber bundle break when they are wound onto a bobbin, taken out from the bobbin, aligned to be combined with plastic, etc., or woven. Problems such as ``single thread breakage'' and tangles were likely to occur. Carbon fiber obtained by conventional methods does not cause "single thread breakage" even when sizing
could not be prevented. According to the method of the present invention, the amount of hydrogen chloride can be kept low, making it extremely easy to treat the exhaust gas, and since no moisture is present, there are fewer problems of equipment corrosion. Furthermore, carbonization in an atmosphere using a combination of hydrogen chloride and oxygen has the effect of significantly reducing the occurrence of "single fiber breakage" in the resulting carbon fibers. Therefore, the high-strength carbon fiber obtained by the present invention can be used without sizing even under severe handling conditions.
Alternatively, it can be fully used without special sizing. The present invention will be specifically described below based on Examples and Comparative Examples. Examples 1 to 12 and Comparative Examples 1 to 13 Acrylonitrile content 95%, 9000 denier,
0.1g/6000 filament PAN fiber in air
After heating at 250° C. for 1 hour under d tension to make it flame resistant, it was heated to 1400° C. and carbonized at various hydrogen chloride and oxygen concentrations in the HCl-O 2 -N 2 atmosphere shown in Table 1. The time required for carbonization was 2 minutes. The properties of the obtained carbon fibers are shown in Table 1. The number of occurrences of "single thread breakage" is as shown in Figure 1.
The carbon fiber bundle 2 is pulled out from the center of the bobbin 1 and guided to the guide roll 3 located L = 50 cm away from the center of the bobbin 1.
A load of 500 g was applied using a weight 4, and then an air flow of 20 m/sec (at room temperature) was blown onto the center of the carbon fiber bundle 2 from a position of m = 10 cm using a blower 5 for 30 seconds. The number of occurrences was measured.
【表】【table】
【表】
第1表に示されるように本発明の範囲にある塩
化水素濃度、酸素濃度および不活性ガス雰囲気中
で加熱処理された炭素繊維は、その他の条件下で
加熱処理された炭素繊維と比較して引張強さおよ
び曲げ強度に優れ、かつ「単糸切れ」数が少な
い。
以上の説明からも明らかなように、ポリアクリ
ロニトリル繊維を酸化性雰囲気中で耐炎化した
後、特定濃度のHCl−O2−不活性ガス雰囲気中で
加熱する本発明の方法により得られる炭素繊維
は、従来の方法によるものに比して、強度に優れ
ると共に著しく「単糸切れ」の発生数が少ないこ
とから、取り扱い性に優れたものであることがわ
かる。[Table] As shown in Table 1, carbon fibers heat-treated in hydrogen chloride concentration, oxygen concentration, and inert gas atmosphere within the range of the present invention are different from carbon fibers heat-treated under other conditions. In comparison, it has excellent tensile strength and bending strength, and has fewer "single thread breaks." As is clear from the above explanation, the carbon fiber obtained by the method of the present invention in which polyacrylonitrile fiber is made flame resistant in an oxidizing atmosphere and then heated in an HCl-O 2 -inert gas atmosphere at a specific concentration is Compared to the conventional method, it has excellent strength and the number of occurrences of "single yarn breakage" is significantly lower, indicating that it is easier to handle.
第1図は「単糸切れ」の測定方法を示す図。
1:ボビン、2:炭素繊維束、3:ガイドロー
ル、4:錘、5:ブロア。
FIG. 1 is a diagram showing a method for measuring "single yarn breakage." 1: bobbin, 2: carbon fiber bundle, 3: guide roll, 4: weight, 5: blower.
Claims (1)
中で加熱して耐炎化した後、塩化水素0.2〜10容
量%、酸素0.2〜4容量%および不活性ガスを含
有する雰囲気中で加熱することを特徴とする炭素
繊維の製造方法。1. Polyacrylonitrile fibers are heated in an oxidizing atmosphere to make them flame resistant, and then heated in an atmosphere containing 0.2 to 10% by volume of hydrogen chloride, 0.2 to 4% by volume of oxygen, and an inert gas. Carbon fiber manufacturing method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3824883A JPS59168129A (en) | 1983-03-10 | 1983-03-10 | Production of carbon fiber |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3824883A JPS59168129A (en) | 1983-03-10 | 1983-03-10 | Production of carbon fiber |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS59168129A JPS59168129A (en) | 1984-09-21 |
JPS6250574B2 true JPS6250574B2 (en) | 1987-10-26 |
Family
ID=12520000
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3824883A Granted JPS59168129A (en) | 1983-03-10 | 1983-03-10 | Production of carbon fiber |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59168129A (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60110925A (en) * | 1983-11-15 | 1985-06-17 | Asahi Chem Ind Co Ltd | Manufacture of high-performance carbon fiber |
JPS60252719A (en) * | 1984-05-30 | 1985-12-13 | Asahi Chem Ind Co Ltd | Production of carbon fiber having high elongation |
JPS61225373A (en) * | 1985-03-27 | 1986-10-07 | 東邦レーヨン株式会社 | Carbon fiber bundle |
JPS61231265A (en) * | 1985-03-30 | 1986-10-15 | 旭化成株式会社 | Production of high performance carbon fiber |
-
1983
- 1983-03-10 JP JP3824883A patent/JPS59168129A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS59168129A (en) | 1984-09-21 |
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