JPH0323650B2 - - Google Patents

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Publication number
JPH0323650B2
JPH0323650B2 JP58191293A JP19129383A JPH0323650B2 JP H0323650 B2 JPH0323650 B2 JP H0323650B2 JP 58191293 A JP58191293 A JP 58191293A JP 19129383 A JP19129383 A JP 19129383A JP H0323650 B2 JPH0323650 B2 JP H0323650B2
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JP
Japan
Prior art keywords
elongation
fiber
temperature
fibers
strength
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 - Lifetime
Application number
JP58191293A
Other languages
Japanese (ja)
Other versions
JPS6088128A (en
Inventor
Soji Nakatani
Yoshitaka Imai
Hiroaki Yoneyama
Yoshiteru Tanuki
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.)
Mitsubishi Chemical Corp
Original Assignee
Mitsubishi Rayon 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 Mitsubishi Rayon Co Ltd filed Critical Mitsubishi Rayon Co Ltd
Priority to JP58191293A priority Critical patent/JPS6088128A/en
Priority to DE8484903763T priority patent/DE3485026D1/en
Priority to EP84903763A priority patent/EP0159365B1/en
Priority to PCT/JP1984/000486 priority patent/WO1985001752A1/en
Publication of JPS6088128A publication Critical patent/JPS6088128A/en
Priority to US07/401,775 priority patent/US5051216A/en
Publication of JPH0323650B2 publication Critical patent/JPH0323650B2/ja
Priority to US07/682,383 priority patent/US5281477A/en
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

〔技術分野〕 本発明は、高強度かつ高弾性である炭素繊維の
製造法に関する。 〔背景技術〕 近年、炭素繊維複合材料は、スポーツ用途、宇
宙航空用途、工業用途等に巾広く応用されつつあ
り、その量的拡大はめざましい。このような状況
に対応して、使用される炭素繊維の性能も飛躍的
に向上しつつある。 弾性率に着目すれば、10年前には20ton/mm2前
後であつたものが、数年前には23〜24ton/mm2が
標準となりさらに最近では30ton/mm2前後のもの
が指向されつつあり、今後はこれが主流となる可
能性も指摘されている。 しかしながら、このような弾性率の向上が、も
しも炭素繊維の強度を一定にしたままで達成され
るならば、これは当然のことながら炭素繊維の伸
度の低下をもたらすこととなり、炭素繊維複合材
料を脆弱なものとし、複合材料の信頼性を低下さ
せることとなる。 したがつて高弾性かつ高伸度の炭素繊維、いい
かえれば高伸度であると同時に高強度である炭素
繊維が強く必要とされる現状にある。 従来の弾性率の向上の方法は炭素化温度すなわ
ち最終熱処理温度を上昇させることであつた。し
かしながら、この方法では弾性率の向上と共に強
度は低下し、したがつて炭素繊維の伸度が低下す
るという欠点があつた。第1図はかかる事情を説
明する炭素化温度と得られる炭素繊維の物性との
関係を示す相関図である。第1図によれば、炭素
化温度の上昇にともない、弾性率は曲線Aのごと
く上昇するが、強度ならびに炭素繊維の密度は、
B,Cのごとく低下する。 例えば28ton/mm3の弾性率を保とうとすれば炭
素化温度は約1800℃が必要であるが、この温度で
は1300℃に比較して強度は100Kg/mm3以上低下し、
高強度はとうてい達成できない。炭素化温度の上
昇にともなうこのような強度の低下は、密度の低
下と良く対応しており、炭素化温度上昇の過程で
強度の低下をもたらすミクロな空孔が繊維中に発
生するためであると推定される。 〔発明の目的〕 炭素化温度を上昇させて高弾性繊維を得るとい
う従来技術では、高弾性と高強度を同時に満足す
る炭素繊維を得ることは困難であり、このような
目標に対しては新規な焼成技術の確立が必要とな
る。 この目標に対して鋭意検討の結果、本発明者等
は新規焼成方法を見出し、本発明を完成するに至
つた。 〔発明の構成〕 本発明の要旨とするところは、単繊維デニール
が0.1〜1.1デニールのアクリル繊維を用い、繊維
の密度が1.22g/cm3に上昇するまでに3%以上、
さらに1.22g/cm3以後において1%以上の伸長を
加えて耐炎化処理を完了し、ついで不活性雰囲気
中300〜800℃の温度で3%以上の伸長を加え、さ
らに不活性雰囲気中1300〜1600℃の温度で緊張下
に処理を行つて、繊維直径が1〜6μ、ストラン
ド強度が460Kg/mm2以上、ストランド弾性率が
28t/mm2以上、ストランド伸度が1.60%以上、密
度が1.76g/cm3以上の炭素繊維の製造方法を提供
することにある。 以下に本発明について、さらに詳細に説明す
る。 本発明におけるアクリル繊維とは、アクリロニ
トリル(AN)を85wt%以上含有する単独重合体
または共重合体より得られる繊維である。 共重合成分としては、ANと共重合し得るすべ
ての単量体を意味し、その代表例を列挙すれば、
ビニルエステル類、アクリル酸エステル類、メタ
クリル酸エステル類、アクリル酸類、メタクリル
酸類、イタコン酸類等である。 このような単独または共重合体を得る方法とし
ては、均一溶液重合、水溶液におけるレドツクス
重合、不均一系における懸濁重合乳化重合等を用
いることができる。 本発明におけるアクリル繊維は1.1デニール以
下、好ましくは1.0デニール以下の繊度を有する
ことが不可欠である。 本発明者等は、このような細繊度のアクリル繊
維を用いることにより、初めて本発明の特性を有
する炭素繊維が得られることを見出した。 細繊度のアクリル繊維を焼成して炭素繊維を得
ることは、例えば特開昭49−94924号公報や特開
昭57−42934号公報等によつて公知である。しか
しながら、このような公知文献には、本発明の特
性を有する炭素繊維ならびにその製造法を示唆す
る記載は全く認められない。 これは、このような細繊度のアクリル繊維を用
いても、焼成条件が不適当であれば、本発明の特
性を有する炭素繊維が得られないことを示してお
り、本発明はかかる細デニールのアクリル繊維と
本発明の焼成条件との結合によつて初めて達成さ
れるものであることを証明するものである。 本発明における細繊度のアクリル繊維は、湿式
紡糸、乾式紡糸等の通常のアクリル繊維の紡糸方
式を利用することによつて製造される。例えば通
常の湿式紡糸においては紡糸、延伸、水洗、乾燥
緻密化の後で、必要に応じて乾熱延伸、スチーム
延伸等の2次延伸を施す。また該アクリル繊維は
不純物、内部ボイド、クレーズやクラツク等の表
面欠陥を含まないことが好ましい。 このようにして得られたアクリル繊維は、本発
明の焼成方法に従つて耐炎化、第1次炭素化、お
よび第2次炭素化処理が施される。 耐炎化処理は通常は空気の如き酸素−窒素の混
合雰囲気中で行われるか一酸化窒素や亜硫酸ガス
を使用しても良い。耐炎化処理時の温度は200〜
350℃の範囲が適当である。 本発明の耐炎化処理に際しては、耐炎化処理過
程における繊維の密度が1.22g/cm3に到達するま
でに3%以上、好ましくは10%以上の伸長を与え
た後に、さらに1.22g/cm3以降の密度域において
1%以上の伸長を加えて耐炎化処理を完了するこ
とが必要である。 耐炎化過程において、このような伸長を加える
ことにより繊維の微細構造に乱れをまつたく生じ
ることなく耐炎化は完了され、本発明の炭素繊維
を得ることが可能となる。 繊維にこのような伸長挙動を与える方法として
は、例えば繊維を多数個の回転ロールと接触させ
ると共に、回転ロールの速度を所定の伸長プロフ
アイルとなるように設定することにより達成でき
る。耐炎化処理が施された繊維は、次いて窒素ガ
ス、アルゴンガス等の不活性雰囲気中300〜800℃
の温度範囲において、第1次炭素化処理を行うに
あたり3%以上、好ましくは5%以上の伸長がさ
らに加えられる。この処理において伸長率が3%
未満であれば、所定の弾性率ならびに強度を得る
ことが困難となる。また、温度が300℃未満なら
びに800℃を越える場合は処理効果が見出せない。
処理は通常数十秒から数分間行われる。 第1次炭素化処理に引き続き、第2炭素化処理
すなわち最終熱処理が不活性雰囲気中1300〜1600
℃好ましくは1300〜1500℃の温度範囲で緊張下に
数十秒〜数分間行われる。この熱処理において、
処理過程における最高温度が1300℃未満であれ
ば、所定の弾性率を得ることができない。一方、
最高温度が1600℃を越えると強度ならびに密度が
低下し所定の値以下となる。 また、熱処理時における温度プロフアイルは、
1000℃前後よりなだらかに上昇して最高温度に到
達するように設定されることが好ましい。また、
熱処理時において繊維に与えられる張力は250
mg/デニール以上、好ましくは350mg/デニール
以上である必要がある。張力がこの値より低い場
合は所定の弾性率を得ることは困難となる。 本発明は上記した方法を採用することによつ
て、繊維直径が1〜6μ、ストランド強度が460
Kg/mm2以上好ましくは500Kg/mm2以上、ストラン
ド弾性率が28t/mm2以上、ストランド伸度が1.60
%以上好ましくは1.7%以上より好ましくは1.8%
以上、密度が1.76g/cm3以上より好ましくは1.78
g/cm3以上の炭素繊維を容易に製造したるに至
る。 以下、実施例により本発明を具体的に説明す
る。 ストランド強度、ストランド弾性率は
JISR7601の方法により測定した。密度は密度勾
配管法により測定した。 ストランド伸度は ストランド強度/ストランド弾性率×100(%) で示されるものである。 炭素繊維の直径はレーザー法により測定した。
アクリル繊維の配向度は2θ=17゜(Cu−kα線使
用)の反射における方位角方向の散乱強度分布の
半価巾H1/2(deg)より次式により求める。 =180−H1/2/180×100(%) 実施例 1 アクリロニトリル98wt%、アクリル酸メチル
1wt%、メタクリル酸1wt%の組成を有する比粘
度〔ηsp〕=0.20の重合体をジメチルホルムアミド
を溶媒として湿式紡糸を行い、引き続き湯浴上5
倍に延伸し、水洗後乾燥して更に乾熱170℃で1.3
倍に延伸して0.8デニールの繊度を有するフイラ
メント数9000のアクリル繊維を得た。X線回析よ
り求められる繊維の配向度は90.3%であつた。
このアクリル繊維を220℃−240℃−260℃の3段
階の温度プロフアイルを有する熱風循環型の耐炎
化炉を60分間通過せしめて耐炎化処理を行うに際
し、繊維の密度が1.22g/cm3に達するまでに20%
の伸長を加え、その後1.25g/cm3に達するまでに
さらに3%の伸長を加えて耐炎化処理を終了し
た。 次に耐炎化繊維を純粋なN2気流中600℃の第1
炭素化炉中を3分間通過せしめるに際して10%の
伸長を加え、さらに同雰囲気中表1の最高温度を
有する第2炭素化炉中において400mg/デニール
の張力下に熱処理を行い、表1の諸物性を有する
炭素繊維を得た。
[Technical Field] The present invention relates to a method for producing carbon fibers having high strength and high elasticity. [Background Art] In recent years, carbon fiber composite materials have been widely applied to sports, aerospace, industrial applications, etc., and their quantitative expansion is remarkable. In response to this situation, the performance of the carbon fibers used is also improving dramatically. If we focus on the modulus of elasticity, 10 years ago it was around 20ton/ mm2 , but a few years ago it became standard at 23-24ton/ mm2 , and more recently, the trend has been around 30ton/ mm2 . It has been pointed out that this may become mainstream in the future. However, if such an improvement in the elastic modulus is achieved while the strength of the carbon fiber remains constant, this will naturally lead to a decrease in the elongation of the carbon fiber, and the carbon fiber composite material This makes the composite material brittle and reduces the reliability of the composite material. Therefore, there is a strong need for carbon fibers that have high elasticity and high elongation, or in other words, carbon fibers that have both high elongation and high strength. The conventional method of improving the elastic modulus has been to increase the carbonization temperature, that is, the final heat treatment temperature. However, this method has the drawback that as the modulus of elasticity increases, the strength decreases, and therefore the elongation of the carbon fibers decreases. FIG. 1 is a correlation diagram showing the relationship between the carbonization temperature and the physical properties of the obtained carbon fiber to explain this situation. According to Figure 1, as the carbonization temperature increases, the elastic modulus increases as shown by curve A, but the strength and density of carbon fibers increase.
It decreases like B and C. For example, in order to maintain an elastic modulus of 28 ton/mm 3 , the carbonization temperature must be approximately 1800°C, but at this temperature the strength decreases by more than 100 kg/mm 3 compared to 1300°C.
High intensities are simply not achievable. This decrease in strength as the carbonization temperature rises corresponds well to the decrease in density, and is due to the generation of microscopic pores in the fibers that cause a decrease in strength during the process of increasing the carbonization temperature. It is estimated to be. [Purpose of the Invention] It is difficult to obtain carbon fibers that satisfy both high elasticity and high strength using the conventional technology of increasing the carbonization temperature to obtain high elastic fibers. It is necessary to establish a suitable firing technology. As a result of intensive studies toward this goal, the present inventors discovered a new firing method and completed the present invention. [Structure of the Invention] The gist of the present invention is to use acrylic fibers with a single fiber denier of 0.1 to 1.1 denier, and to increase the fiber density by 3% or more until the fiber density rises to 1.22 g/cm 3 .
Furthermore, after 1.22 g/ cm3 , an elongation of 1% or more is added to complete the flame-retardant treatment, then an elongation of 3% or more is added at a temperature of 300 to 800°C in an inert atmosphere, and a further elongation of 1300 to Processed under tension at a temperature of 1600℃, the fiber diameter is 1 to 6μ, the strand strength is 460Kg/mm2 or more, and the strand elastic modulus is
The object of the present invention is to provide a method for producing carbon fiber having a strand elongation of 28 t/mm 2 or more, a strand elongation of 1.60% or more, and a density of 1.76 g/cm 3 or more. The present invention will be explained in more detail below. The acrylic fiber in the present invention is a fiber obtained from a homopolymer or copolymer containing 85 wt% or more of acrylonitrile (AN). Copolymerizable components refer to all monomers that can be copolymerized with AN, and representative examples include:
These include vinyl esters, acrylic esters, methacrylic esters, acrylic acids, methacrylic acids, and itaconic acids. As a method for obtaining such a homopolymer or a copolymer, homogeneous solution polymerization, redox polymerization in an aqueous solution, suspension polymerization or emulsion polymerization in a heterogeneous system, etc. can be used. It is essential that the acrylic fiber in the present invention has a fineness of 1.1 denier or less, preferably 1.0 denier or less. The present inventors have discovered that carbon fibers having the characteristics of the present invention can be obtained for the first time by using acrylic fibers having such fineness. It is known to obtain carbon fibers by firing fine acrylic fibers, for example, as disclosed in Japanese Patent Application Laid-open No. 49-94924 and Japanese Patent Application Laid-open No. 57-42934. However, in such known documents, there is no description that suggests the carbon fiber having the characteristics of the present invention and its manufacturing method. This shows that even if acrylic fibers with such a fine denier are used, carbon fibers having the characteristics of the present invention cannot be obtained if the firing conditions are inappropriate. This proves that this can only be achieved by combining acrylic fibers and the firing conditions of the present invention. The fine-grained acrylic fiber in the present invention is produced by using a conventional acrylic fiber spinning method such as wet spinning or dry spinning. For example, in normal wet spinning, after spinning, stretching, washing with water, and drying and densification, secondary stretching such as dry heat stretching or steam stretching is performed as necessary. Further, it is preferable that the acrylic fiber does not contain impurities, internal voids, and surface defects such as crazes and cracks. The acrylic fiber thus obtained is subjected to flameproofing, primary carbonization, and secondary carbonization treatments according to the firing method of the present invention. The flameproofing treatment is usually carried out in an oxygen-nitrogen mixed atmosphere such as air, or nitrogen monoxide or sulfur dioxide gas may be used. The temperature during flameproofing treatment is 200~
A range of 350°C is appropriate. In the flame-retardant treatment of the present invention, the fibers are elongated by 3% or more, preferably 10% or more, until the fiber density reaches 1.22 g/cm 3 in the flame-retardant treatment process, and then further elongated to 1.22 g/cm 3 . In the subsequent density range, it is necessary to add elongation of 1% or more to complete the flame resistance treatment. By applying such elongation during the flameproofing process, flameproofing is completed without causing any disturbance to the fine structure of the fibers, making it possible to obtain the carbon fiber of the present invention. Such elongation behavior can be imparted to the fibers by, for example, bringing the fibers into contact with a number of rotating rolls and setting the speed of the rotating rolls to provide a predetermined elongation profile. The flame-resistant fibers are then heated at 300-800℃ in an inert atmosphere such as nitrogen gas or argon gas.
In the temperature range of 3% or more, preferably 5% or more, elongation is further applied during the primary carbonization treatment. In this process, the elongation rate is 3%
If it is less than that, it will be difficult to obtain a predetermined elastic modulus and strength. Furthermore, no treatment effect can be found when the temperature is below 300°C or above 800°C.
The process usually takes from several tens of seconds to several minutes. Following the first carbonization treatment, the second carbonization treatment, that is, the final heat treatment, is performed at 1300 to 1600 in an inert atmosphere.
It is preferably carried out under tension at a temperature range of 1,300 to 1,500 degrees Celsius for several tens of seconds to several minutes. In this heat treatment,
If the maximum temperature during the treatment process is less than 1300°C, it is not possible to obtain a predetermined elastic modulus. on the other hand,
When the maximum temperature exceeds 1600°C, the strength and density decrease and become below a predetermined value. In addition, the temperature profile during heat treatment is
It is preferable to set the temperature so that the temperature rises gradually from around 1000°C to reach the maximum temperature. Also,
The tension applied to the fiber during heat treatment is 250
It needs to be at least mg/denier, preferably at least 350 mg/denier. If the tension is lower than this value, it will be difficult to obtain a predetermined elastic modulus. By employing the method described above, the present invention has a fiber diameter of 1 to 6 μm and a strand strength of 460 μm.
Kg/mm 2 or more, preferably 500 Kg/mm 2 or more, strand elastic modulus 28t/mm 2 or more, strand elongation 1.60
% or more, preferably 1.7% or more, preferably 1.8%
or more, the density is 1.76 g/cm 3 or more, preferably 1.78
Carbon fibers of g/cm 3 or more can be easily produced. Hereinafter, the present invention will be specifically explained with reference to Examples. Strand strength and strand elastic modulus are
Measured according to the method of JISR7601. Density was measured by density gradient tube method. Strand elongation is expressed as strand strength/strand elastic modulus x 100 (%). The diameter of the carbon fibers was measured by a laser method.
The degree of orientation of the acrylic fibers is determined from the half-width H1/2 (deg) of the scattering intensity distribution in the azimuthal direction in reflection at 2θ=17° (using Cu-kα radiation) using the following equation. =180−H1/2/180×100(%) Example 1 Acrylonitrile 98wt%, methyl acrylate
A polymer with a specific viscosity [ηsp] = 0.20 having a composition of 1 wt% and 1 wt% methacrylic acid was wet-spun using dimethylformamide as a solvent, and then spun on a hot water bath for 5 minutes.
Stretch it twice, wash it with water, dry it, and heat it to 1.3
An acrylic fiber with a filament count of 9000 and a fineness of 0.8 denier was obtained by stretching it twice. The degree of fiber orientation determined by X-ray diffraction was 90.3%.
When this acrylic fiber was subjected to flame-retardant treatment by passing through a hot air circulation type flame-retardant furnace with a three-step temperature profile of 220°C - 240°C - 260°C for 60 minutes, the density of the fiber was 1.22 g/cm 3 20% to reach
, and then further elongation of 3% until reaching 1.25 g/cm 3 to complete the flame-retardant treatment. The flame-retardant fibers were then heated to 600°C in a pure N2 stream.
A 10% elongation was applied during passing through the carbonization furnace for 3 minutes, and heat treatment was performed under a tension of 400 mg/denier in a second carbonization furnace having the maximum temperature shown in Table 1 in the same atmosphere. Carbon fibers with physical properties were obtained.

【表】 実施例 2 実施例1と同様にして、但し耐炎化処理時の伸
長率ならびに第1炭素化炉内での温度と伸長率を
変更して焼成を実施した。なお、第1炭素化炉の
温度は550℃、第2炭素化炉の最高温度は1450℃、
張力は380mg/デニールとした。得られた炭素繊
維の諸物性を表2に示す。
[Table] Example 2 Firing was carried out in the same manner as in Example 1, except that the elongation rate during the flameproofing treatment and the temperature and elongation rate in the first carbonization furnace were changed. The temperature of the first carbonization furnace is 550℃, the maximum temperature of the second carbonization furnace is 1450℃,
The tension was 380 mg/denier. Table 2 shows the physical properties of the obtained carbon fiber.

【表】 なお、耐炎化伸長率()は、繊維の密度が
1.22g/cm3に至るまでの伸長率であり、同()
は繊維の密度が1.22〜1.25g/cm3の範囲における
伸長率である。 実施例 3 実施例1と同様にして、但し原液吐出量ならび
に延伸倍率を変更して表3に示す繊維を有するア
クリル繊維を得た。 これ等のアクリル繊維を実施例1と同一の条件
にて焼成を行つた。この際最終熱処理時における
最高温度は1450℃、張力は400mg/デニールとし
た。得られた炭素繊維の諸物性を表3に示す。
[Table] The flame resistant elongation rate () is determined by the fiber density.
The elongation rate is up to 1.22g/ cm3 , and the same ()
is the elongation rate in the range of fiber density from 1.22 to 1.25 g/cm 3 . Example 3 Acrylic fibers having the fibers shown in Table 3 were obtained in the same manner as in Example 1, except that the discharge amount of the stock solution and the stretching ratio were changed. These acrylic fibers were fired under the same conditions as in Example 1. At this time, the maximum temperature during the final heat treatment was 1450°C, and the tension was 400 mg/denier. Table 3 shows the physical properties of the obtained carbon fiber.

【表】 実施例 4 実施例1において第1炭素化炉の温度を変えて
焼成を行い、表4に示す結果を得た。
[Table] Example 4 In Example 1, firing was performed by changing the temperature of the first carbonization furnace, and the results shown in Table 4 were obtained.

〔発明の効果〕〔Effect of the invention〕

本発明で得られた炭素繊維は高弾性かつ高強力
であるため航空機一次構造材、釣竿、ゴルフシヤ
フト等のスポーツ用途、高速遠心分離機、ロボツ
ト等の工業用途、地上高速輸送体等広範囲な用途
に使用することが可能である。
The carbon fiber obtained by the present invention has high elasticity and high strength, so it has a wide range of applications such as primary structural materials for aircraft, sports applications such as fishing rods and golf shafts, industrial applications such as high-speed centrifuges and robots, and high-speed ground transportation vehicles. It is possible to use it for

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

第1図は、従来法による炭素化温度で得られる
炭素繊維の物性との関係を示す相関図である。 A……弾性率、B……強度、C……密度。
FIG. 1 is a correlation diagram showing the relationship with the physical properties of carbon fibers obtained at carbonization temperatures according to the conventional method. A...Modulus, B...Strength, C...Density.

Claims (1)

【特許請求の範囲】[Claims] 1 単繊維デニールが0.1〜1.1デニールのアクリ
ル繊維を用い、繊維の密度が1.22g/cm3に上昇す
るまでに3%以上、さらに1.22g/cm3以後におい
て1%以上の伸長を加えて耐炎化処理を完了し、
ついで不活性雰囲気中300〜800℃の温度で3%以
上の伸長を加え、さらに不活性雰囲気中1300〜
1600℃の温度で緊張下に処理を行つて、繊維直径
が1〜6μ、ストランド強度が460Kg/mm2以上、ス
トランド弾性率が28t/mm2以上、ストランド伸度
が1.60%以上、密度が1.76g/cm3以上の炭素繊維
を製造することを特徴とする高強度・高弾性炭素
繊維の製造法。
1 Using acrylic fibers with a single fiber denier of 0.1 to 1.1 denier, flame resistance is achieved by elongating 3% or more until the fiber density rises to 1.22 g/cm 3 and then elongating 1% or more after 1.22 g/cm 3 complete the conversion process,
Then, elongation of 3% or more is applied at a temperature of 300 to 800°C in an inert atmosphere, and further elongation of 1300 to 800°C in an inert atmosphere.
Treated under tension at a temperature of 1600℃, the fiber diameter is 1 to 6μ, the strand strength is 460Kg/ mm2 or more, the strand elastic modulus is 28t/mm2 or more, the strand elongation is 1.60% or more, and the density is 1.76. A method for producing high-strength and high-elasticity carbon fibers, characterized by producing carbon fibers with a weight of g/cm 3 or more.
JP58191293A 1983-10-13 1983-10-13 Manufacturing method for high strength and high modulus carbon fiber Granted JPS6088128A (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
JP58191293A JPS6088128A (en) 1983-10-13 1983-10-13 Manufacturing method for high strength and high modulus carbon fiber
DE8484903763T DE3485026D1 (en) 1983-10-13 1984-10-12 CARBON FIBERS WITH HIGH STRENGTH AND HIGH ELASTICITY MODULE AND THEIR PRODUCTION PROCESS.
EP84903763A EP0159365B1 (en) 1983-10-13 1984-10-12 Carbon fibers with high strength and high modulus, and process for their production
PCT/JP1984/000486 WO1985001752A1 (en) 1983-10-13 1984-10-12 Carbon fibers with high strength and high modulus, and process for their production
US07/401,775 US5051216A (en) 1983-10-13 1989-09-01 Process for producing carbon fibers of high tenacity and modulus of elasticity
US07/682,383 US5281477A (en) 1983-10-13 1991-04-09 Carbon fibers having high tenacity and high modulus of elasticity and process for producing the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58191293A JPS6088128A (en) 1983-10-13 1983-10-13 Manufacturing method for high strength and high modulus carbon fiber

Publications (2)

Publication Number Publication Date
JPS6088128A JPS6088128A (en) 1985-05-17
JPH0323650B2 true JPH0323650B2 (en) 1991-03-29

Family

ID=16272155

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58191293A Granted JPS6088128A (en) 1983-10-13 1983-10-13 Manufacturing method for high strength and high modulus carbon fiber

Country Status (1)

Country Link
JP (1) JPS6088128A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009084390A1 (en) 2007-12-30 2009-07-09 Toho Tenax Co., Ltd. Processes for producing flameproof fiber and carbon fiber

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6233826A (en) * 1985-08-07 1987-02-13 Asahi Chem Ind Co Ltd Production of high-strength and high-modulus carbon fiber
JPS6233825A (en) * 1985-08-07 1987-02-13 Asahi Chem Ind Co Ltd Production of high-strength and high modulus carbon fiber

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5725418A (en) * 1980-07-16 1982-02-10 Mitsubishi Rayon Co Ltd Preparation of low-density carbon fiber
JPS5742925A (en) * 1980-08-22 1982-03-10 Toho Rayon Co Ltd Production of high-performance carbon fiber strand
JPS58136834A (en) * 1982-02-03 1983-08-15 Mitsubishi Rayon Co Ltd Manufacturing method for high-performance carbon fiber
JPS58136838A (en) * 1982-02-08 1983-08-15 Mitsubishi Rayon Co Ltd Production of high-performance carbon fiber
JPS58144128A (en) * 1982-02-18 1983-08-27 Mitsubishi Rayon Co Ltd Preparation of carbon fiber having high performance
JPS58115121A (en) * 1982-12-23 1983-07-08 Mitsubishi Rayon Co Ltd Acrylic carbon fiber
JPS58115122A (en) * 1982-12-23 1983-07-08 Mitsubishi Rayon Co Ltd Acrylic flameproofed yarn

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009084390A1 (en) 2007-12-30 2009-07-09 Toho Tenax Co., Ltd. Processes for producing flameproof fiber and carbon fiber

Also Published As

Publication number Publication date
JPS6088128A (en) 1985-05-17

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