JPH0681221A - Production of carbon fiber - Google Patents

Production of carbon fiber

Info

Publication number
JPH0681221A
JPH0681221A JP26049992A JP26049992A JPH0681221A JP H0681221 A JPH0681221 A JP H0681221A JP 26049992 A JP26049992 A JP 26049992A JP 26049992 A JP26049992 A JP 26049992A JP H0681221 A JPH0681221 A JP H0681221A
Authority
JP
Japan
Prior art keywords
fiber
yarn
pitch
carbonization
temperature
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.)
Granted
Application number
JP26049992A
Other languages
Japanese (ja)
Other versions
JP2930167B2 (en
Inventor
Yutaka Arai
豊 荒井
Mitsuaki Matsumoto
光昭 松本
Yoshitoshi Nishikawa
俊寿 西川
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.)
Nippon Steel Corp
Nippon Steel Chemical and Materials Co Ltd
Original Assignee
Nippon Steel Corp
Nippon Steel Chemical 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 Nippon Steel Corp, Nippon Steel Chemical Co Ltd filed Critical Nippon Steel Corp
Priority to JP4260499A priority Critical patent/JP2930167B2/en
Publication of JPH0681221A publication Critical patent/JPH0681221A/en
Priority to US08/437,921 priority patent/US5595720A/en
Application granted granted Critical
Publication of JP2930167B2 publication Critical patent/JP2930167B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Inorganic Fibers (AREA)

Abstract

PURPOSE:To provide a process for improving the productivity of the graphitization process for a pitch-based carbon fiber and the quality of the product. CONSTITUTION:A pitch fiber produced by using a mesophase pitch as a raw material is oxidized in an oxidizing atmosphere containing nitrogen dioxide and oxygen, baked in an inert gas atmosphere at 350-400 deg.C for >=10min and continuously carbonized at 800-1300 deg.C. In this processed, the baking of the fiber is carried out while applying a tension of 50-2,500g/mm<2> to the fiber. The yarn is cut at a broken part of the yarn before winding the carbon fiber on a bobbin or receiving in a receptor.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は炭素繊維の製造方法に関
するものであり、特に種々のピッチから炭素繊維を糸切
れなく安定して、大量迅速に製造する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing carbon fibers, and more particularly to a method for producing carbon fibers from various pitches in a stable manner without yarn breakage, and in large quantities and rapidly.

【0002】[0002]

【従来の技術】炭素繊維は、比強度および比弾性率の高
い材料で近年、航空宇宙分野、自動車工業、その他の工
業分野で、強くて軽い素材として注目を浴びている。
2. Description of the Related Art Carbon fiber is a material having a high specific strength and a high specific elastic modulus, and has recently attracted attention as a strong and light material in the aerospace field, the automobile industry and other industrial fields.

【0003】このような分野では高強度、高弾性率であ
りながら安価な材料が望まれている。
In such fields, inexpensive materials having high strength and high elastic modulus are desired.

【0004】現在、炭素繊維はポリアクリルニトリル
(PAN)を原料とするPAN系炭素繊維とピッチ類を
原料とするピッチ系炭素繊維が製造されているが、現状
では高強度、高弾性率の高性能炭素繊維としては主にP
AN系炭素繊維が使用されている。
Currently, PAN-based carbon fibers made from polyacrylonitrile (PAN) and pitch-based carbon fibers made from pitches are manufactured as carbon fibers, but at present, they have high strength and high elastic modulus. Performance carbon fiber is mainly P
AN-based carbon fiber is used.

【0005】しかしながら、PAN系炭素繊維はさらに
高弾性率化するには限界があり、また、その原料となる
PANが高価であり、PANから得られる炭素繊維収率
が低いことなどもあって、炭素繊維の価格が高価となら
ざるを得ないという問題がある。
However, the PAN-based carbon fiber has a limit to further increase the elastic modulus, the PAN as a raw material thereof is expensive, and the yield of the carbon fiber obtained from the PAN is low. There is a problem that the price of carbon fiber is inevitably high.

【0006】そこで、近年、炭素繊維収率が高く、高弾
性率化が容易なメソフェーズピッチを原料とするピッチ
系炭素繊維の高性能化の検討が種々行なわれている。
[0006] Therefore, in recent years, various studies have been conducted to improve the performance of pitch-based carbon fibers made of mesophase pitch, which has a high yield of carbon fibers and is easily made to have a high elastic modulus.

【0007】しかしながらピッチ繊維は脆弱であり、中
間工程品である不融化繊維もその強度が5〜10kg/
mm2と著しく脆いために、その繊維が100〜10
0,000本集合した、不融化繊維糸条はその取扱が難
しく、糸切れしやすく長尺な繊維の製造が困難であった
り毛羽立ちが多いとの問題がある。
However, the pitch fiber is fragile and the strength of the infusible fiber which is an intermediate step product is 5 to 10 kg /
Since the fiber is extremely brittle at mm 2 , the fiber is 100 to 10
The infusible fiber yarns, which are aggregated into 30,000 fibers, are difficult to handle, and there are problems that the yarns are easily broken and long fibers are difficult to produce, and fuzz is often generated.

【0008】また、不融化繊維糸条を線状に繰り出し
て、炭化あるいは黒鉛化を行うと、特開平4―9122
9号公報に開示されるように、炭化あるいは黒鉛化の際
に繊維糸条内の単糸が融着し、糸条が剛直になったりす
るなど製品品質を著しく低下するという問題があった。
Further, when the infusible fiber yarn is drawn out linearly and carbonized or graphitized, it is disclosed in JP-A-4-9122.
As disclosed in Japanese Patent Publication No. 9, there is a problem that the single yarn in the fiber yarn is fused at the time of carbonization or graphitization, and the yarn becomes rigid, so that the product quality is significantly deteriorated.

【0009】かかる問題点に関し、特公昭62―202
81号公報では不融化後、400〜650℃の範囲で初
期炭化を行い、この初期炭化繊維をハンドリングする方
法が記載されている。
Regarding such a problem, Japanese Patent Publication No. 62-202
Japanese Patent No. 81 discloses a method in which after infusibilization, initial carbonization is performed in the range of 400 to 650 ° C, and the initial carbonized fiber is handled.

【0010】一般にピッチ繊維を不融化し、炭化処理を
行うと、特公昭62―20281号公報に記載されるよ
うに、炭化処理温度が500〜600℃の間で繊維の破
断伸度が著しく向上する点が存在する。
Generally, when pitch fibers are infusibilized and carbonized, as shown in Japanese Patent Publication No. 62-20281, the breaking elongation of the fibers is remarkably improved at a carbonization temperature of 500 to 600 ° C. There is a point to do.

【0011】この破断伸度が大きいことを利用してこの
温度領域で炭化を行い糸条のハンドリングを行うことが
知られている。
It is known that carbonization is performed in this temperature range to handle the yarn by utilizing the fact that the breaking elongation is large.

【0012】さらに特開昭60―126324号公報に
は、繊維の破断伸度を2.5%を超えるまで加熱し、炭
化を行い、その後繊維糸条を緊張下に更に高温、雰囲気
で炭化、黒鉛化を行いフィラメント揃いのよい炭素繊維
束を製造する方法が記載されている。
Further, in Japanese Patent Application Laid-Open No. 60-126324, the fiber is heated to a breaking elongation of more than 2.5% for carbonization, and then the fiber yarn is carbonized under tension at higher temperature and atmosphere. A method for producing a carbon fiber bundle having good filament alignment by graphitization is described.

【0013】一方、不融化処理時間を短縮するなど生産
性の改善、あるいは炭素繊維物性の改善として不融化ガ
スに二酸化窒素を用いる方法が特開昭60―25962
9号公報に、あるいは二酸化窒素さらに水蒸気を混合す
る方法が特開平2―6618号公報に記載されている。
On the other hand, there is a method of using nitrogen dioxide as an infusibilizing gas to improve productivity such as shortening the infusibilizing treatment time or to improve physical properties of carbon fiber.
No. 9 or Japanese Patent Laid-Open No. 2-6618 discloses a method of mixing nitrogen dioxide and steam.

【0014】不融化ガスに二酸化窒素ガスを混合したガ
スを用いることにより、従来一般的に行われている空気
による不融化に比べ不融化時間を著しく短縮する事が可
能となる。
By using a gas in which nitrogen dioxide gas is mixed with the infusible gas, the infusibilization time can be remarkably shortened as compared with the conventional infusibilization by air.

【0015】しかしながら、不融化ガスに二酸化窒素を
用いた場合、従来一般的に知られている400〜650
℃の範囲で初期炭化を行っても、繊維の破断伸度が向上
するものの、この範囲では破断強度が低く、糸切れが生
ずるなど、糸条のハンドリング性が改善されないという
問題があった(図1)。
However, when nitrogen dioxide is used as the infusible gas, it is generally known to be 400 to 650.
Even if initial carbonization is performed in the range of ℃, although the breaking elongation of the fiber is improved, there is a problem that the handling strength of the yarn is not improved in such a range that the breaking strength is low and yarn breakage occurs (Fig. 1).

【0016】また、繊維の収縮のために、繊維の揃いが
悪く物性の発現が不安定であったり、黒鉛化工程での糸
条の破断が生じるために生産性の低下を引き起こしたり
した。
Further, due to the shrinkage of the fibers, the uniformity of the fibers is poor and the development of the physical properties is unstable, and the yarn breaks in the graphitization process, which causes a decrease in the productivity.

【0017】黒鉛化工程は温度が2000〜3000℃
で数秒から数分という極短時間、糸条を線状に搬送させ
ながら行なうのが一般的である。
In the graphitization process, the temperature is 2000 to 3000 ° C.
Generally, the yarn is conveyed linearly for a very short time of several seconds to several minutes.

【0018】この際、生産性を上げるために一台の黒鉛
化炉に数本から数100本の糸条を通じるのが一般的で
あり、この糸条は黒鉛化炉の前後に設置されたローラー
によって駆動される。
At this time, in order to improve the productivity, it is common to pass several to several hundred yarns through one graphitizing furnace, and these yarns were installed before and after the graphitizing furnace. Driven by rollers.

【0019】駆動ローラーは設備を簡略化するために、
一台のローラーで複数の糸条を搬送しており、複数本の
糸条の内一本でも破断が生じると、全糸条の搬送を中止
し破断糸条の復旧を行なう。
The drive roller is provided in order to simplify the equipment.
A single roller conveys a plurality of yarns, and if even one of the plurality of yarns breaks, the conveyance of all yarns is stopped and the broken yarns are restored.

【0020】このため、一旦炉内に停止した繊維は製品
とすることができず、生産性を著しく低下することにな
る。
Therefore, the fiber once stopped in the furnace cannot be made into a product, and the productivity is remarkably reduced.

【0021】このため、黒鉛化工程での糸条の破断を起
こさないための技術の開発が望まれている。
Therefore, it is desired to develop a technique for preventing breakage of the yarn in the graphitization process.

【0022】[0022]

【発明が解決しようとする課題】本発明は、二酸化窒素
ガスを用いて得られた不融化繊維を、さらに炭化、黒鉛
化する際に、糸条の糸切れ、融着をなくするなどのハン
ドリング性を改善し、さらに炭化、黒鉛化処理工程の生
産性と品質を改善する方法を提供することにある。
DISCLOSURE OF THE INVENTION The present invention is directed to handling such as eliminating yarn breakage and fusion of yarn when carbonizing and graphitizing infusible fibers obtained by using nitrogen dioxide gas. The object of the present invention is to provide a method of improving the productivity and further improving the productivity and quality of the carbonization and graphitization treatment steps.

【0023】[0023]

【課題を解決するための手段】本発明はメソフェースピ
ッチを原料とするピッチ繊維を二酸化窒素と酸素を含む
酸化性ガス雰囲気で酸化処理し、この酸化繊維を350
〜400℃で10min以上不活性化雰囲気で焼成し、
その後、800〜1300℃の温度で連続的に炭化を行
なうときに、糸条に50〜2500g/mm2の張力を
加えながら焼成することを特徴とする炭素繊維の製造方
法、および800〜1300℃の温度で連続的に炭化を
行ない、ボビンあるいは受器に繊維を連続的に受け取る
際に、ボビンあるいは受器に受け取る前に、糸条の剛
直、一部破断箇所にて糸条を強制的に切断することを特
徴とする炭素繊維の製造方法である。
According to the present invention, pitch fibers made from mesophase pitch as a raw material are oxidized in an oxidizing gas atmosphere containing nitrogen dioxide and oxygen, and the oxidized fibers are heated to 350 ° C.
Firing at ~ 400 ° C for 10 min or more in an inert atmosphere,
After that, when continuously carbonizing at a temperature of 800 to 1300 ° C., a method for producing a carbon fiber, which comprises firing while applying a tension of 50 to 2500 g / mm 2 to the yarn, and 800 to 1300 ° C. When the fiber is continuously carbonized at the temperature of, and the fiber is continuously received by the bobbin or the receiver, the yarn is forced to be rigid or partially broken before it is received by the bobbin or the receiver. It is a method for producing a carbon fiber, which is characterized by cutting.

【0024】以下、本発明の内容を詳細に説明する。The contents of the present invention will be described in detail below.

【0025】本発明の炭素繊維の出発原料であるピッチ
としては、コールタール、コールタールピッチ等の石炭
系ピッチ、石炭液化ピッチ、エチレンタールピッチ、流
動接触触媒分解残渣油から得られるデカントオイルピッ
チ等の石油系ピッチ、あるいはナフタレン等から触媒な
どを用いて作られる合成ピッチ等、各種のピッチが挙げ
られる。
The pitch which is the starting material of the carbon fiber of the present invention includes coal-based pitch such as coal tar and coal tar pitch, coal liquefied pitch, ethylene tar pitch, decant oil pitch obtained from fluid catalytic cracking residual oil, and the like. Various pitches such as petroleum-based pitches described above, or synthetic pitches made from naphthalene using a catalyst or the like can be used.

【0026】本発明の炭素繊維に使用されるメソフェー
ズピッチは、前記のピッチを従来公知の方法でメソフェ
ーズを発生させたものである。
The mesophase pitch used in the carbon fiber of the present invention is the above-mentioned pitch in which the mesophase is generated by a conventionally known method.

【0027】メソフェーズピッチは、紡糸した際のピッ
チ繊維の配向性が高いものが望ましく、このためメソフ
ェーズ含有量は40%以上、より好ましくは70%以上
含有するものが望ましい。
The mesophase pitch is preferably such that the pitch fibers are highly oriented when spun, and therefore the mesophase content is preferably 40% or more, more preferably 70% or more.

【0028】また、本発明で用いるメソフェーズピッチ
は軟化点が200〜400℃、より好ましくは250〜
350℃のものがよい。
The softening point of the mesophase pitch used in the present invention is 200 to 400 ° C., more preferably 250 to 400 ° C.
A temperature of 350 ° C is preferable.

【0029】前記メソフェーズピッチをこれまで知られ
ている方法にて溶融紡糸を行うことによりピッチ繊維が
得られる。
Pitch fibers are obtained by melt spinning the mesophase pitch by a method known so far.

【0030】例えば、前記メソフェーズピッチを粘度1
00ポイズ〜2000ポイズを示す温度で、口径0.1
mm〜0.5mmのキャピラリーから、圧力0.1〜1
00kg/cm2程度で押し出しながら100〜200
0m/minの引き取り速度で延伸し、繊維径が5〜2
0μmのピッチ繊維を得る。
For example, the mesophase pitch has a viscosity of 1
A caliber of 0.1 at a temperature of 00 poise to 2000 poise
mm ~ 0.5mm capillary, pressure 0.1 ~ 1
100 to 200 while extruding at about 00 kg / cm 2.
Stretched at a take-up speed of 0 m / min and a fiber diameter of 5 to 2
A pitch fiber of 0 μm is obtained.

【0031】つぎにピッチ繊維は、糸条(繊維束)とし
て、二酸化窒素濃度が2〜10体積%、酸素濃度が2〜
20体積%、必要に応じて水蒸気を2〜10体積%含
み、残りのガスを窒素等の不活性ガスとした酸化性ガス
雰囲気下で、温度100〜320℃、処理時間30〜3
00min、好ましくは40〜200minの条件で不
融化する。
Next, the pitch fiber has a nitrogen dioxide concentration of 2 to 10% by volume and an oxygen concentration of 2 to 2 as a yarn (fiber bundle).
20% by volume, 2 to 10% by volume of water vapor as needed, and an oxidizing gas atmosphere in which the remaining gas is an inert gas such as nitrogen, temperature 100 to 320 ° C., treatment time 30 to 3
It is infusibilized under the condition of 00 min, preferably 40 to 200 min.

【0032】この不融化糸を350℃以上400℃未満
の温度で10min以上窒素ガス等の不活性雰囲気で最
初の炭化(一次炭化)を行なうことが肝要である。
It is essential that the infusible yarn is first carbonized (primary carbonization) at a temperature of 350 ° C. or higher and lower than 400 ° C. for 10 min or longer in an inert atmosphere such as nitrogen gas.

【0033】図1に不融化繊維を炭化温度を変えて30
分間炭化した際の単繊維の破断伸びと、炭化繊維糸条の
破断強度を測定した結果を示した。
FIG. 1 shows the infusible fiber at 30 different carbonization temperatures.
The results of measuring the breaking elongation of the single fiber and the breaking strength of the carbonized fiber yarn when carbonized for a minute are shown.

【0034】単繊維の破断の伸びの平均値は400〜6
50℃程度の炭化温度で最大値を示すが、炭化繊維糸条
の破断強度は不融化糸から390℃の焼成温度で緩やか
に向上し、400℃以上で急激に強度が減少することが
わかる。
The average value of elongation at break of single fiber is 400 to 6
Although it shows the maximum value at the carbonization temperature of about 50 ° C., it is understood that the breaking strength of the carbonized fiber yarn gradually increases from the infusibilized yarn at the firing temperature of 390 ° C., and sharply decreases at 400 ° C. or higher.

【0035】原因は定かではないが、単繊維の平均強度
および破断伸度は炭化温度の上昇と共に向上するもの
の、そのばらつきは大きくなる。
Although the cause is not clear, although the average strength and the elongation at break of the single fiber are improved as the carbonization temperature is increased, the variations are increased.

【0036】400℃未満の炭化温度では単繊維の強
度、破断伸び共に400〜500℃程度の炭化糸に比べ
小さいもののばらつきは少なく、糸条にした際の強度発
現率が高いものと考えられる。
At a carbonization temperature of less than 400 ° C., both the strength and the elongation at break of the single fiber are smaller than those of the carbonized yarn of about 400 to 500 ° C., but there is little variation, and it is considered that the strength development rate when formed into a yarn is high.

【0037】しかも、400℃以上の炭化温度では、炭
化の過程で繊維長さが約3.2%、500℃では4.5
%程度収縮する。
Moreover, at a carbonization temperature of 400 ° C. or higher, the fiber length is about 3.2% during the carbonization process, and at 500 ° C., it is 4.5%.
Shrinks about%.

【0038】したがって、糸条内の単繊維の長さが炭化
時の収縮により不均一となり、繊維の揃いが乱れ炭化繊
維糸条の強度が著しく低下したり、最終製品である炭素
繊維あるいは黒鉛化繊維の品質を著しく低下させる。
Therefore, the length of the monofilament in the yarn becomes non-uniform due to shrinkage during carbonization, the alignment of the fibers is disturbed, the strength of the carbonized fiber yarn is remarkably reduced, and the final product carbon fiber or graphitized. It significantly reduces the quality of the fiber.

【0039】このため、800〜1300℃までの温度
で炭化(2次炭化)を行なう際に、50〜2500g/
mm2、より好ましくは60〜1000g/mm2の張力
を加えながら焼成を行なうことにより、400℃以上の
炭化温度で生じる繊維長さ方向の収縮を均一にすること
が初めて可能となり、糸揃いの改善された糸条を得るこ
とができる。
Therefore, when carbonization (secondary carbonization) is performed at a temperature of 800 to 1300 ° C., 50 to 2500 g /
By performing the firing while applying a tension of mm 2 , more preferably 60 to 1000 g / mm 2 , it becomes possible for the first time to make uniform shrinkage in the fiber length direction that occurs at a carbonization temperature of 400 ° C. or higher, so that the yarn alignment An improved yarn can be obtained.

【0040】2次炭化を行なう際の張力が50g/mm
2未満では繊維糸条の揃いは改善されず、また2500
g/mm2超では2次炭化中に糸条が破断し易くなる。
The tension when carrying out the secondary carbonization is 50 g / mm.
If it is less than 2 , the alignment of the fiber threads is not improved, and it is 2500
If it exceeds g / mm 2 , the yarn is likely to break during secondary carbonization.

【0041】一方350℃より1次炭化温度が低い場
合、800〜1300℃の温度で5秒〜2分という、糸
条を連続的に炭化(2次炭化)を行なうと炭化の際に生
じる分解物により、繊維の融着あるいは剛直といった問
題が生じる。
On the other hand, when the primary carbonization temperature is lower than 350 ° C., when the yarn is continuously carbonized (secondary carbonization) at a temperature of 800 to 1300 ° C. for 5 seconds to 2 minutes, decomposition occurs during carbonization. Depending on the object, problems such as fusion of fibers or rigidity occur.

【0042】このため、少なくとも350℃以上の温度
で10min以上、不融化繊維を一旦炭化する必要があ
る。
Therefore, it is necessary to once carbonize the infusible fiber at a temperature of at least 350 ° C. for 10 minutes or more.

【0043】二酸化窒素ガスを含む不融化で得られた不
融化繊維にはある種の窒素化合物が生成しており、ある
程度の温度と時間をかけて炭化する必要があり、そうで
ない場合、急速に炭化を行なうことにより繊維の融着、
剛直が見られる。
The infusibilized fiber obtained by the infusibilization containing nitrogen dioxide gas contains a certain amount of nitrogen compound and needs to be carbonized at a certain temperature and for a certain period of time. Fusion of fibers by carbonization,
Rigidity can be seen.

【0044】2次炭化の温度が800℃より低い場合、
2次炭化糸条の強度が低く、次の黒鉛化工程での取扱が
難しく、また、1300℃を超える場合、2次炭化繊維
の弾性率が大きくなり、ボビンへ2次炭化糸を巻取った
場合に、毛羽立ち等の問題が生じる。
When the temperature of the secondary carbonization is lower than 800 ° C.,
The strength of the secondary carbonized yarn is low, it is difficult to handle in the next graphitization process, and when it exceeds 1300 ° C., the elastic modulus of the secondary carbonized fiber becomes large, and the secondary carbonized yarn was wound on the bobbin. In this case, problems such as fuzzing occur.

【0045】以上のような製造条件の設定で2次炭化糸
を得ることで、次工程の黒鉛化工程での生産性は極めて
向上する。
By obtaining the secondary carbonized yarn by setting the production conditions as described above, the productivity in the next graphitization step is extremely improved.

【0046】しかしながら、ピッチ系炭素繊維では、脆
弱なピッチ繊維を出発原料に製造するために、どうして
も、炭化糸糸条に欠陥、例えば、繊維同志の融着、ある
いは剛直が生じたり、繊維糸条の一部が傷つき、一部的
に破断している箇所を皆無にする事が極めて難しい。
However, in the case of pitch-based carbon fibers, since fragile pitch fibers are used as a starting material, defects in carbonized yarns are inevitable, for example, fusion between fibers or stiffness occurs, or fiber yarns are produced. It is extremely difficult to get rid of the part that is partially damaged and partially broken.

【0047】そこで、2次炭化糸をケンス等の収納容
器、あるいはボビンに巻取る前に糸条を、目視あるいは
光学的検出装置により繊維糸条にある一部欠陥箇所を検
出し、ここで糸条を強制的に切断し、欠陥個所を取り除
くことにより次工程である黒鉛化工程には、欠陥を全く
含まない炭化糸条を供給することが可能となり、黒鉛化
工程の生産性がさらに向上し、その結果炭素繊維製品の
生産性が著しく向上することが可能となる。
Therefore, before winding the secondary carbonized yarn on a container such as a can or a bobbin, the yarn is detected visually or by an optical detection device to detect a partial defect in the fiber yarn. By forcibly cutting the filaments and removing the defective parts, it becomes possible to supply carbonized filament yarns that do not contain any defects in the next step, the graphitization step, further improving the productivity of the graphitization step. As a result, the productivity of carbon fiber products can be significantly improved.

【0048】[0048]

【実施例】実施例で求めた諸物性は次の方法で測定し
た。
EXAMPLES Various physical properties obtained in the examples were measured by the following methods.

【0049】(1)軟化点 軟化点は、フローテスターを用いてハーゲン・ポアズイ
ユ式から算出される見掛けの粘度が20,000ポイズ
となる温度である。
(1) Softening point The softening point is the temperature at which the apparent viscosity calculated from the Hagen-Poiseuille equation using a flow tester becomes 20,000 poise.

【0050】(2)トルエン不溶分、ピリジン不溶分 トルエン不溶分、ピリジン不溶分はJIS―K―242
5(1978年)に示された方法に準じて測定した。
(2) Toluene-insoluble matter and pyridine-insoluble matter Toluene-insoluble matter and pyridine-insoluble matter are JIS-K-242.
5 (1978).

【0051】(3)単糸破断伸び及び黒鉛化糸強度、弾
性率 JIS―R―7601(1986年)に示された方法に
準じて測定した。
(3) Single yarn breaking elongation, graphitized yarn strength and elastic modulus It was measured according to the method described in JIS-R-7601 (1986).

【0052】(4)繊維糸条の破断強度 繊維糸条の破断強度は3000本の繊維からなる糸条を
測定長が1mになるように、繊維糸条両端にタブを接着
剤で固定した試料を多数作成し、これを引張速度50m
m/minの速度で引張り、引張破断荷重を求めた。
(4) Breaking strength of fiber thread The breaking strength of the fiber thread is a sample in which tabs are fixed to both ends of the fiber thread with an adhesive so that the measurement length of the thread consisting of 3000 fibers is 1 m. Create a large number of and pull it at a pulling speed of 50 m
Tensile breaking load was determined by pulling at a speed of m / min.

【0053】原料としてキノリン不溶分を除去した、軟
化点80℃のコールタールピッチを、触媒を用い直接水
素化を行った。
Coal tar pitch having a softening point of 80 ° C. from which quinoline insoluble matter was removed as a raw material was directly hydrogenated using a catalyst.

【0054】この水素化処理ピッチを常圧下480℃で
熱処理した後、低沸点分を除きメソフェーズピッチを得
た。このピッチは、軟化点が304℃、トルエン不溶分
が85重量%、ピリジン不溶分が40重量%、メソフェ
ーズ含有量が95%であった。
This hydrotreated pitch was heat-treated at 480 ° C. under normal pressure, and the low boiling point was removed to obtain mesophase pitch. This pitch had a softening point of 304 ° C., a toluene insoluble content of 85% by weight, a pyridine insoluble content of 40% by weight, and a mesophase content of 95%.

【0055】このピッチを用いて、キャピラリー径0.
14mm、ノズルホール数3000のノズルパックを有
する紡糸機を用いて、メソフェーズピッチの粘度800
ポイズで糸径13μmのピッチ繊維を紡糸し、このピッ
チ繊維を油剤を用いずに、エアーサッカーで集束させな
がらケンス収納した。
Using this pitch, the capillary diameter of 0.
Using a spinning machine having a nozzle pack with 14 mm and 3000 nozzle holes, the viscosity of the mesophase pitch is 800.
A pitch fiber having a yarn diameter of 13 μm was spun by poise, and the pitch fiber was stored in a can while being focused with an air sucker without using an oil agent.

【0056】このピッチ繊維をケンス(容器)に収納し
たまま、空気に二酸化窒素ガスを5体積%、および水蒸
気を5体積%添加した酸化ガスを、ケンス下部から吹き
込みながら、150℃から300℃まで1℃/minで
昇温し、そのまま300℃に30分保持して不融化繊維
を得た。
While the pitch fiber was stored in a can (container), an oxidizing gas obtained by adding 5% by volume of nitrogen dioxide gas and 5% by volume of steam to the air was blown from the lower part of the can to 150 ° C. to 300 ° C. The temperature was raised at 1 ° C./min, and the temperature was kept at 300 ° C. for 30 minutes to obtain infusible fibers.

【0057】この不融化繊維を収納したケンスをそのま
ま、窒素ガス雰囲気下で、不融化繊維を10℃/min
で昇温し、300℃〜600℃まで昇温しその温度で3
0min保持し、一次炭化を行なった。
The can containing the infusible fiber is left as it is under a nitrogen gas atmosphere to remove the infusible fiber at 10 ° C./min.
At 300 ° C to 600 ° C at that temperature for 3
It was held for 0 min to carry out primary carbonization.

【0058】得られた繊維の単糸の破断伸びと1mの長
さでの繊維糸条の破断強度を測定した結果を図1に示し
た。
The breaking elongation of the single yarn of the obtained fiber and the breaking strength of the fiber yarn at a length of 1 m were measured and the results are shown in FIG.

【0059】上記1次炭化糸を入口温度が500℃、出
口温度が1100℃、窒素ガス雰囲気の長さ2mの炉
に、ケンスから繰り出した繊維糸条を線状に、張力を1
00g/mm2、速度4m/minの速度で通しながら
2次炭化を行ない得られた2次炭化繊維をボビンに巻と
った。
The primary carbonized yarn was introduced into a furnace having an inlet temperature of 500 ° C., an outlet temperature of 1100 ° C., and a length of 2 m in a nitrogen gas atmosphere.
Secondary carbonization was carried out while passing through at a speed of 00 g / mm 2 and a speed of 4 m / min, and the obtained secondary carbonized fiber was wound on a bobbin.

【0060】一次炭化温度が350℃未満のものは、2
次炭化の際に糸条が剛直となり糸条の破断が生じた。
If the primary carbonization temperature is less than 350 ° C., 2
During the subsequent carbonization, the yarn became rigid and fractured.

【0061】一方、一次炭化温度が350℃以上のもの
は糸条の剛直はないものの、一次炭化温度が400℃以
上のものは毛羽立ちが非常に多い2次炭化糸であった。
On the other hand, the yarns having a primary carbonization temperature of 350 ° C. or higher were not stiff, but the ones having a primary carbonization temperature of 400 ° C. or higher were secondary carbonized yarns with much fuzz.

【0062】つぎに1次炭化温度が390℃のものにつ
いて、張力を変化させながら2次炭化を行なった。
Next, secondary carbonization was carried out with the primary carbonization temperature of 390 ° C. while changing the tension.

【0063】図2に示すようにケンス1から繰り出した
1次炭化糸2は3のダンサーローラーによって張力を与
え、2次炭化炉4に通した。
As shown in FIG. 2, the primary carbonized yarn 2 fed from the can 1 was given tension by the dancer roller 3 and passed through the secondary carbonization furnace 4.

【0064】炉の出口とボビンに糸条を巻取る巻取り機
2との間には、直径20mmのロール7に約90度の角
度で糸条を巻き付け、図3に示すようにこのロールの上
面をレーザー光線による糸条の一部破断、あるいは剛直
部を検出する糸傷検出機8を設置し、これを2箇所通過
したあと、ボビン9に2次炭化繊維を巻取った。
Between the outlet of the furnace and the winding machine 2 for winding the yarn around the bobbin, the yarn is wound around a roll 7 having a diameter of 20 mm at an angle of about 90 degrees, and as shown in FIG. A yarn flaw detector 8 for detecting a partial breakage of a yarn or a rigid portion on the upper surface by a laser beam was installed, and after passing through two places, a secondary carbonized fiber was wound on a bobbin 9.

【0065】その後2次炭化繊維はボビンから糸条を巻
き返しながら2300℃の温度で、張力を300g/m
2を与えながら、30秒間アルゴン雰囲気中で黒鉛化
を行い黒鉛化繊維を得た。
After that, the secondary carbonized fiber was wound around the bobbin and the tension was 300 g / m at a temperature of 2300.degree.
Graphitized fiber was obtained by performing graphitization in an argon atmosphere for 30 seconds while giving m 2 .

【0066】結果を第1表、第2表に示した。The results are shown in Tables 1 and 2.

【0067】[0067]

【表1】 [Table 1]

【0068】[0068]

【表2】 [Table 2]

【0069】[0069]

【発明の効果】本発明により、2次炭化の際に張力を付
与することにより、又2次炭化後、糸傷部を除外するこ
とにより、長時間連続に通糸が可能であり、生産性良く
炭素繊維を製造出来る他、得られた繊維は毛羽立ちもな
く美麗であった。
EFFECTS OF THE INVENTION According to the present invention, it is possible to continuously pass a yarn for a long time by applying a tension at the time of the secondary carbonization, or by eliminating a yarn scratched portion after the secondary carbonization. In addition to being able to produce carbon fiber well, the obtained fiber was beautiful without fluffing.

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

【図1】炭化処理における処理温度と強度・伸びとの関
係図。
FIG. 1 is a diagram showing a relationship between a treatment temperature and strength / elongation in carbonization treatment.

【図2】本発明の生産工程の1例を示す図。FIG. 2 is a diagram showing an example of a production process of the present invention.

【図3】本発明における糸傷検出の説明図。FIG. 3 is an explanatory diagram of yarn flaw detection according to the present invention.

【符号の説明】 1 ケンス 2 1次炭化糸 3 ダンサーローラー 4 2次炭化炉 5 フィードローラー 6 2次炭化糸 7 ロール 8 糸傷検出機 9 ボビン 10 糸傷部 11 レーザー光線[Explanation of symbols] 1 cans 2 primary carbonized yarn 3 dancer roller 4 secondary carbonization furnace 5 feed roller 6 secondary carbonized yarn 7 roll 8 yarn flaw detector 9 bobbin 10 yarn wound portion 11 laser beam

───────────────────────────────────────────────────── フロントページの続き (72)発明者 西川 俊寿 姫路市広畑区富士町1番地 新日本製鐵株 式会社広畑製鐵所内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Toshihisa Nishikawa 1 Fuji-machi, Hirohata-ku, Himeji City Nippon Steel Corporation Hirohata Works

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 メソフェースピッチを原料とするピッチ
繊維糸条をボビンに巻きとるか、または糸条のまま繰り
出し可能に堆積し、これらをそのまま二酸化窒素と酸素
を含む酸化性ガス雰囲気で酸化不融化処理し、及び35
0〜400℃未満で10min以上不活性雰囲気で焼成
して1次炭化し、その後、糸条を線状に繰り出して80
0〜1300℃の温度で5秒〜2分間連続搬送させなが
ら2次炭化を行なうときに、糸条に50〜2500g/
mm2の張力を加えながら2次炭化することを特徴とす
る炭素繊維の製造方法。
1. A pitch fiber thread made of mesophase pitch as a raw material is wound around a bobbin or is deposited so that the thread can be fed out as it is, and these are directly oxidized in an oxidizing gas atmosphere containing nitrogen dioxide and oxygen. Fusion treatment, and 35
It is fired in an inert atmosphere at 0 to less than 400 ° C. for 10 minutes or more to perform primary carbonization, and then the filament is fed out in a linear shape to 80
When secondary carbonization is carried out while continuously conveying at a temperature of 0 to 1300 ° C. for 5 seconds to 2 minutes, 50 to 2500 g /
A method for producing a carbon fiber, which comprises secondary carbonizing while applying a tension of mm 2 .
【請求項2】 800〜1300℃の温度で連続的に2
次炭化を行ない、ボビンあるいは受器に繊維を連続的に
受け取る際に、ボビンあるいは受器に受け取る前に、糸
条の剛直又は一部破断箇所を検出し、その箇所にて糸条
を強制的に切断することを特徴とする、請求項1記載の
炭素繊維の製造方法。
2. Continuously at a temperature of 800 to 1300 ° C.
When the subsequent carbonization is performed and the fibers are continuously received by the bobbin or the receiver, the rigid or partially broken part of the yarn is detected before the fiber is received by the bobbin or the receiver, and the yarn is forced at that position. The method for producing a carbon fiber according to claim 1, wherein the carbon fiber is cut into pieces.
JP4260499A 1992-09-04 1992-09-04 Carbon fiber production method Expired - Lifetime JP2930167B2 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP4260499A JP2930167B2 (en) 1992-09-04 1992-09-04 Carbon fiber production method
US08/437,921 US5595720A (en) 1992-09-04 1995-05-09 Method for producing carbon fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4260499A JP2930167B2 (en) 1992-09-04 1992-09-04 Carbon fiber production method

Publications (2)

Publication Number Publication Date
JPH0681221A true JPH0681221A (en) 1994-03-22
JP2930167B2 JP2930167B2 (en) 1999-08-03

Family

ID=17348822

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4260499A Expired - Lifetime JP2930167B2 (en) 1992-09-04 1992-09-04 Carbon fiber production method

Country Status (1)

Country Link
JP (1) JP2930167B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017210705A (en) * 2016-05-27 2017-11-30 帝人株式会社 Method for producing ultrafine carbon fiber
JP2019094603A (en) * 2017-11-24 2019-06-20 帝人株式会社 Mesophase pitch-containing fiber bundle, stabilized mesophase pitch-containing fiber bundle, and manufacturing method of them

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60259629A (en) * 1984-05-31 1985-12-21 Nippon Oil Co Ltd Production of graphitized pitch fiber
JPS6220281A (en) * 1985-07-17 1987-01-28 川崎製鉄株式会社 Induction heating control for continuous casting
JPS62184125A (en) * 1986-02-10 1987-08-12 Toa Nenryo Kogyo Kk Production of carbon yarn and graphite yarn

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60259629A (en) * 1984-05-31 1985-12-21 Nippon Oil Co Ltd Production of graphitized pitch fiber
JPS6220281A (en) * 1985-07-17 1987-01-28 川崎製鉄株式会社 Induction heating control for continuous casting
JPS62184125A (en) * 1986-02-10 1987-08-12 Toa Nenryo Kogyo Kk Production of carbon yarn and graphite yarn

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017210705A (en) * 2016-05-27 2017-11-30 帝人株式会社 Method for producing ultrafine carbon fiber
JP2019094603A (en) * 2017-11-24 2019-06-20 帝人株式会社 Mesophase pitch-containing fiber bundle, stabilized mesophase pitch-containing fiber bundle, and manufacturing method of them

Also Published As

Publication number Publication date
JP2930167B2 (en) 1999-08-03

Similar Documents

Publication Publication Date Title
JP5161604B2 (en) Carbon fiber manufacturing method
JP4370034B2 (en) Pitch fiber bundle, pitch-based carbon fiber bundle and method for producing the same
US4975262A (en) Three dimensional woven fabrics of pitch-derived carbon fibers
WO2019087766A1 (en) Carbon fiber bundle and method for producing same
JP2930167B2 (en) Carbon fiber production method
US5595720A (en) Method for producing carbon fiber
JP2930166B2 (en) Carbon fiber production method
JP2695355B2 (en) Carbon fiber production method
JPS6220281B2 (en)
JPH038808A (en) Production of pitch-based carbon fiber
JP2708684B2 (en) Pitch-based carbon fiber bundle
JP2665118B2 (en) Method for producing fine pitch-based carbon fiber and spinning nozzle
JPS6278220A (en) Production of ribbon-like carbon fiber
JPS63303123A (en) Pitch-based carbon fiber and production thereof
JPH0617319A (en) Production of pitch-based carbon fiber
JPH05287617A (en) Production of pitch carbon fiber
JPH01282327A (en) Oxidation of pitch fiber
JPS58214526A (en) Carbon fiber bundle of high strength and elongation
JPH05171519A (en) Production of pitch carbon fiber
JPH02216220A (en) Production of pitch-base carbon fiber
JPH01282330A (en) Production of pitch-based carbon fiber
JPH05295619A (en) Production of pitch-based carbon fiber
JPH06166912A (en) Production of carbon fiber
JPS59150115A (en) Production of carbon fiber
JPH01282324A (en) Production of pitch-based carbon fiber

Legal Events

Date Code Title Description
A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 19970826

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313111

R360 Written notification for declining of transfer of rights

Free format text: JAPANESE INTERMEDIATE CODE: R360

R371 Transfer withdrawn

Free format text: JAPANESE INTERMEDIATE CODE: R371

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313111

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090521

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090521

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100521

Year of fee payment: 11

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110521

Year of fee payment: 12

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110521

Year of fee payment: 12

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120521

Year of fee payment: 13

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130521

Year of fee payment: 14

EXPY Cancellation because of completion of term
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130521

Year of fee payment: 14