JPH0860448A - Production of pitch-based carbon yarn - Google Patents

Production of pitch-based carbon yarn

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Publication number
JPH0860448A
JPH0860448A JP24768095A JP24768095A JPH0860448A JP H0860448 A JPH0860448 A JP H0860448A JP 24768095 A JP24768095 A JP 24768095A JP 24768095 A JP24768095 A JP 24768095A JP H0860448 A JPH0860448 A JP H0860448A
Authority
JP
Japan
Prior art keywords
pitch
yarn
based carbon
silicone oil
fibers
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
JP24768095A
Other languages
Japanese (ja)
Other versions
JP2708055B2 (en
Inventor
Masami Kagizaki
正己 鍵崎
Takeshi Takakura
剛 高倉
Hiroshi Tawara
博志 田原
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 Chemical Corp
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 Chemical Corp filed Critical Mitsubishi Chemical Corp
Priority to JP7247680A priority Critical patent/JP2708055B2/en
Publication of JPH0860448A publication Critical patent/JPH0860448A/en
Application granted granted Critical
Publication of JP2708055B2 publication Critical patent/JP2708055B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE: To produce pitch-based carbon yarn having excellent properties in a continuous filament state by facilitating handleability of fragile yarn and preventing occurrence of adhesion and fusing between mutual yarns and damage on the surface of yarn. CONSTITUTION: In a method for producing pitch-based carbon yarn by subjecting a raw material pitch to melt spinning to give pitch yarn, collecting the pitch yarn, infusibilizing and optionally graphitizing, the pitch yarn during or before the collection is coated with a water emulsion of a silicone oil having 0.1-35wt.% silicone oil concentration as a collecting agent, retained at 50-100 deg.C for 2 minutes to 2 hours in a drying furnace set immediately ahead an infusibilizing furnace or in the first process of the infusibilizing furnace and dried to provide a method for producing pitch-based carbon yarn.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は石炭系ピッチ、石油
系ピッチ、高分子焼成ピッチ等のピッチ類から炭素繊維
を製造する方法に関するものであり、詳しくは繊維の取
扱いを容易にすると同時に繊維相互間の接着や融着のな
い高品質の炭素繊維を得る方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing carbon fibers from pitches such as coal-based pitch, petroleum-based pitch, and polymer-fired pitch. The present invention relates to a method for obtaining a high-quality carbon fiber without adhesion or fusion between the two.

【0002】[0002]

【従来技術】ピッチ系炭素繊維は、通常、原料ピッチを
溶融紡糸し、得られたピッチ繊維を不融化処理及び炭化
処理を行うことによって製造される。ピッチ系炭素繊維
はポリアクリロニトリル系等の炭素繊維に比較して高収
率で工業的に有利に製造できる利点がある反面、ピッチ
繊維が極めて脆弱なため、不融化処理や炭化処理での取
扱いが難しく、これらの工程において繊維の毛羽立ち、
ガイドロールへの捲つき、糸切れ等を起こしやすい。さ
らに不融化処理、炭化処理時にピッチ繊維相互間の接着
や融着が生じ、かつ得られた炭素繊維の表面に損傷を生
じ易い難点がある。
2. Description of the Related Art Pitch-based carbon fibers are usually produced by melt-spinning raw material pitch and subjecting the resulting pitch fibers to infusibilization treatment and carbonization treatment. Pitch-based carbon fibers have the advantage that they can be produced industrially advantageously in high yield compared to polyacrylonitrile-based carbon fibers, but on the other hand, pitch fibers are extremely fragile, so they can be handled by infusibilization treatment or carbonization treatment. Difficult, fiber fluffing in these processes,
Easy to wind around the guide roll or break. Further, there is a problem that the pitch fibers are adhered or fused to each other during the infusibilization treatment or the carbonization treatment, and the surface of the obtained carbon fiber is easily damaged.

【0003】これらの問題点は原料及び製造法の異なっ
たポリアクリロニトリル系炭素繊維の場合とは大きく異
なるものである。即ちポリアクリロニトリル系炭素繊維
の場合は、ジメチルホルムアルデヒドと水の混合物又は
ジメチルスルホキシドと水との混合物を主体とする紡糸
浴中に設置された紡糸ノズルを通して、溶融ポリアクリ
ロニトリルが押出される湿式紡糸法により紡糸され、か
かる湿式紡糸法に於いては、紡糸された各単繊維は紡糸
浴の液体によってその表面を濡らされ、紡糸浴中でトウ
の状態に集束される。紡糸浴中から取り出したトウに対
し、次いで200〜300℃の酸化性雰囲気中で耐炎化
処理を行う際及びその後300〜1400℃の不活性雰
囲気中で炭化処理を行う際にポリエチレングリコール等
を油剤としてトウ(通常500〜1万本程度のフィラメ
ントを集束したもの)の表面に付着させる方法が有効で
あるとされている。
These problems are greatly different from the case of polyacrylonitrile-based carbon fiber having different raw materials and different manufacturing methods. That is, in the case of polyacrylonitrile-based carbon fiber, by a wet spinning method in which molten polyacrylonitrile is extruded through a spinning nozzle installed in a spinning bath mainly containing a mixture of dimethylformaldehyde and water or a mixture of dimethylsulfoxide and water. In such a wet spinning method after spinning, each of the spun single fibers is wetted on its surface by the liquid in the spinning bath and then focused in a tow state in the spinning bath. When the tow taken out from the spinning bath is subjected to a flameproofing treatment in an oxidizing atmosphere at 200 to 300 ° C and then a carbonization treatment in an inert atmosphere at 300 to 1400 ° C, an oil agent such as polyethylene glycol is used. It is said that a method of adhering it to the surface of tow (usually a bundle of about 500 to 10,000 filaments) is effective.

【0004】[0004]

【発明が解決しようとする課題】ところがこれらのポリ
アクリロニトリル系炭素繊維の集束剤として好適な油剤
をピッチ繊維に適用しても、ピッチ繊維はポリアクリロ
ニトリル繊維に比べ、熱や力などの物理的な力にも弱
く、又ポリアクリロニトリルのように重合しているわけ
でもないので化学的にもはるかに不安定であり、その殆
どがピッチ繊維の一部を溶解したり、繊維同志が接着ま
たは融着し剛直になる等の欠点を生じる。
However, even if an oil agent suitable as a sizing agent for these polyacrylonitrile-based carbon fibers is applied to the pitch fiber, the pitch fiber has a physical property such as heat and force as compared with the polyacrylonitrile fiber. It is weak against force, and it is not chemically polymerized like polyacrylonitrile, so it is much more chemically unstable. Most of it melts a part of the pitch fiber, or both fibers bond or fuse. However, it causes defects such as being rigid.

【0005】そこで本発明者らは、このようなピッチ繊
維の集束における難点を解消する方法として、集束剤と
してシリコーン油を用いることについて先に提案を行っ
た。この方法によれば円滑に集束ができるが、操作如何
では場合によりシリコーン油が過度に付着することがあ
り、その場合、集束そのものに不都合はないが、不融化
処理後又は炭化処理後のトウが堅くなりやすく、極端な
場合には融着して開繊しにくくなる場合が生じる。
Therefore, the present inventors have previously proposed the use of silicone oil as a sizing agent as a method for solving such a difficulty in bundling pitch fibers. According to this method, bundling can be performed smoothly, but depending on the operation, silicone oil may adhere excessively in some cases, and in that case, there is no inconvenience in bundling itself, but tow after infusibilization treatment or carbonization treatment It tends to be stiff, and in extreme cases, it may be fused to make it difficult to open the fiber.

【0006】[0006]

【課題を解決するための手段】そこで、本発明者らはこ
れらの問題点を解決するため更に検討を重ねた結果、集
束剤としてシリコーン油の水エマルジョンを用いる方法
が好ましいことを見出し、本発明を完成した。すなわ
ち、本発明の要旨は原料ピッチを溶融紡糸して得られた
ピッチ繊維を集束後、不融化処理、さらに必要に応じて
黒鉛化処理を行うことによりピッチ系炭素繊維を製造す
る方法に於いて、集束の際又は集束前のピッチ繊維に、
集束剤としてシリコーン油の濃度が0.1〜35重量%
であるシリコーン油の水エマルジョンを付着させた後、
更に不融化炉の直前に設けた乾燥炉か不融化炉の最初の
過程において50〜100℃に5分〜2時間保持して乾
燥することを特徴とするピッチ系炭素繊維の製造方法に
存する。
Therefore, as a result of further studies to solve these problems, the present inventors have found that a method of using a water emulsion of silicone oil as a sizing agent is preferable, and the present invention Was completed. That is, the gist of the present invention is a method for producing pitch-based carbon fibers by bundling pitch fibers obtained by melt-spinning raw material pitch, infusibilizing treatment, and further performing graphitization treatment if necessary. , At the time of focusing or on the pitch fiber before focusing,
The concentration of silicone oil as a sizing agent is 0.1 to 35% by weight.
After applying the water emulsion of silicone oil which is
Further, the present invention resides in a method for producing a pitch-based carbon fiber characterized by holding at 50 to 100 ° C. for 5 minutes to 2 hours and drying in the first step of the drying furnace provided immediately before the infusibilizing furnace.

【0007】[0007]

【実施の態様】以下本発明を詳細に説明するに、本発明
に用いられる原料ピッチとしては、コールタールピッ
チ、石炭液化物等の石炭系ピッチ、原油の常圧蒸留残
油、減圧蒸留残油、またはその熱処理物、ナフサ等の熱
分解副生タールの熱処理物等の石油系ピッチ及び合成樹
脂や天然樹脂を乾留することによって得られる高分子焼
成ピッチ等が挙げられる。
BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in detail. Examples of the raw material pitch used in the present invention include coal tar pitch, coal pitch such as coal liquefaction, atmospheric distillation residue of crude oil, and vacuum distillation residual oil. Or a heat-treated product thereof, a petroleum-based pitch such as a heat-treated product of thermal decomposition by-product tar such as naphtha, and a polymer calcined pitch obtained by carbonizing a synthetic resin or a natural resin.

【0008】原料ピッチの溶融紡糸は通常の合成繊維の
乾式法溶融紡糸と同様に行うことができ、特に制限はな
く、溶融した紡糸ピッチを下向きの紡糸口金から気相中
に押し出し冷却固化させる方法を採用する。紡糸口金と
しては吐出孔の孔径が0.1〜0.5mm程度のものを
用いる。紡糸口金の温度は原料ピッチの種類に依存し紡
糸に適当な溶融粘度を考慮して決められるが、通常は2
50〜350℃の範囲が適当である。紡糸口金の下には
保温筒を設けておくと紡糸状態の安定化に有効である。
Melt spinning of the raw material pitch can be carried out in the same manner as dry-method melt spinning of ordinary synthetic fibers, and there is no particular limitation, and the melted spinning pitch is extruded from the downward spinneret into the gas phase and solidified by cooling. To adopt. As the spinneret, one having a discharge hole diameter of about 0.1 to 0.5 mm is used. The temperature of the spinneret depends on the type of raw material pitch and is determined by considering the melt viscosity suitable for spinning.
A range of 50 to 350 ° C is suitable. It is effective to stabilize the spinning state by providing a heat insulation tube below the spinneret.

【0009】本発明においては、紡糸されたピッチ繊維
に集束剤としてシリコーン油の水エマルジョンを付着さ
せるが、具体的なシリコーン油としては、通常ジメチル
ポリシロキサンが用いられるが、このジメチルポリシロ
キサンに種々の基を導入して変性したものも用いられ
る。具体的には、例えばメチルフェニルポリシロキサ
ン、ハイドロジェンポリシロキサンが挙げられるが、そ
の他エポキシ基、エチル、プロピル等のアルキル基、ア
ミノ基、カルボキシル基、アルコール、フェニル基、ポ
リエーテル基の1種又は2種以上で変性したものが用い
られる。また、これらのシリコーン油は、1種又は2種
以上の混合物を用いてもよい。
In the present invention, a water emulsion of silicone oil is adhered to the spun pitch fiber as a sizing agent. As a concrete silicone oil, dimethylpolysiloxane is usually used. Those modified by introducing the above group can also be used. Specific examples thereof include methylphenyl polysiloxane and hydrogen polysiloxane, but also one of an epoxy group, an alkyl group such as ethyl and propyl, an amino group, a carboxyl group, an alcohol, a phenyl group, and a polyether group, or Those modified with two or more kinds are used. Moreover, you may use 1 type or a mixture of 2 or more types of these silicone oils.

【0010】シリコーン油の水エマルジョンは周知の混
合装置例えば高速ミキサ−、コロイドミル、ホモゲナイ
ザー等を用いてシリコーン油が0.1〜35重量%とな
るように水と混合することによって調整される。エマル
ジョンの形成に当たっては、シリコーン油の濃度が高く
なって良好なエマルジョン状態が維持出来なくなる場合
は乳化剤を0.25〜2重量%添加すればよい。乳化剤
は従来公知のものでよく、これにはソルビタン脂肪酸エ
ステル、たとえばソルビタンパルミチン酸エステル、ソ
ルビタンステアリン酸エステル、ポリオキシエチレンソ
ルビタン脂肪酸エステル、ポリオキシエチレンソルビタ
ンカプロン酸エステル、ポリオキシエチレンラウリン酸
エステル、アセチル化モノグリセライド、アセチル化グ
リセリルモノステアレートおよびポリオキシエチレンラ
ノリン誘導体などの非イオン系乳化剤、アルキル硫酸エ
ステル、ナトリウムラウリルサルフェート、ナトリウム
セチルサルフェート、ジアルキルスルホサクシネート、
ジー2−エチルヘキシルスルホサクシネート(ナトリウ
ム塩)などのアニオン系乳化剤、または塩化アルキルピ
リジウムなどのカチオン系乳化剤が例示される。また、
シリコーン油の水エマルジョンに少量の固体微粒子を添
加混合して集束剤として用いてもよい。
A water emulsion of silicone oil is prepared by mixing it with water using a well-known mixing device such as a high speed mixer, a colloid mill or a homogenizer so that the silicone oil becomes 0.1 to 35% by weight. In forming an emulsion, if the concentration of silicone oil is too high to maintain a good emulsion state, an emulsifier may be added in an amount of 0.25 to 2% by weight. The emulsifier may be a conventionally known emulsifier, for example, sorbitan fatty acid ester such as sorbitan palmitate, sorbitan stearic acid ester, polyoxyethylene sorbitan fatty acid ester, polyoxyethylene sorbitan caproic acid ester, polyoxyethylene lauric acid ester, and acetyl. Monoglycerides, non-ionic emulsifiers such as acetylated glyceryl monostearate and polyoxyethylene lanolin derivatives, alkyl sulfates, sodium lauryl sulfate, sodium cetyl sulfate, dialkyl sulfosuccinate,
Examples thereof include anionic emulsifiers such as di-2-ethylhexyl sulfosuccinate (sodium salt), and cationic emulsifiers such as alkylpyridinium chloride. Also,
A small amount of solid fine particles may be added to and mixed with a water emulsion of silicone oil and used as a sizing agent.

【0011】固体微粒子としては、好ましくは炭素質微
粒子、無機酸化物微粒子、無機塩微粒子あるいはこれら
の混合物が用いられるが、具体的には、黒鉛、カーボン
ブラック、シリカ、炭酸カルシウム、酸化チタン、タル
ク、クレー、硫酸バリウム、チタン酸カリ、二硫化モリ
ブデン等の微細な粒子が用いられる。集束剤をピッチ繊
維に付着させる方法としては、スプレーにより吹きつけ
る方法、ローラーに付けて接触させる方法、浸漬させる
方法等がある。繊維に対する付着量は通常2〜14重量
%の範囲であり、特に2〜10重量%が好適である。付
着量が2.0重量%より少ないと紡糸した繊維の十分な
集束状態が維持されず、繊維束のハンドリングが極めて
難しくなりひいては繊維を損傷させる。また油剤の濃度
にもよるが14重量%以上になると不融化処理の際の揮
散が不十分となって繊維上に残存し不融化反応を阻害す
る原因となり、さらに不融化処理に於いて繊維から発生
する低分子量ガスの飛散が十分に行えないためにかえっ
て炭素繊維の強度を低下させる原因となる。
The solid fine particles are preferably carbonaceous fine particles, inorganic oxide fine particles, inorganic salt fine particles or a mixture thereof, and specifically, graphite, carbon black, silica, calcium carbonate, titanium oxide, talc. Fine particles of clay, clay, barium sulfate, potassium titanate, molybdenum disulfide, etc. are used. As a method of attaching the sizing agent to the pitch fibers, there are a method of spraying, a method of contacting with a roller and a method of dipping. The amount of adhesion to the fiber is usually in the range of 2 to 14% by weight, particularly preferably 2 to 10% by weight. If the adhered amount is less than 2.0% by weight, the spun fibers will not be maintained in a sufficiently bundled state, and handling of the fiber bundles will be extremely difficult, and the fibers will be damaged. Also, depending on the concentration of the oil agent, if it is 14% by weight or more, the volatilization during the infusibilization treatment becomes insufficient, and it remains on the fiber and inhibits the infusibilization reaction. Since the generated low molecular weight gas cannot be sufficiently scattered, the strength of the carbon fiber is rather lowered.

【0012】本発明の製造法では、シリコーン油の水エ
マルジョンが付着され、集束されたピッチ繊維はさら
に、不融化炉の直前に設けられた乾燥炉、あるいは不融
化炉の最初の過程で50〜100℃下に5分〜2時間保
持されてピッチ繊維の水付着量を0.1重量%以下に乾
燥される。その後、周知の方法に従って不融化処理及び
炭化処理が行われる。例えば、不融化処理は、繊維を酸
素、オゾン、空気、窒素酸化物、ハロゲン亜硫酸ガス等
の酸化性雰囲気下、150〜360℃の温度に5分〜1
0時間加熱することによって行われる。また炭化処理は
繊維を窒素、アルゴン等の不活性ガス雰囲気下、100
0〜2500℃の温度に0.5分〜10時間加熱するこ
とによって行われる。
In the production method of the present invention, the water-based emulsion of silicone oil is adhered and the pitch fibers bundled are further subjected to a drying furnace immediately before the infusible furnace, or 50 to 50 in the first step of the infusible furnace. It is kept at 100 ° C. for 5 minutes to 2 hours and dried so that the amount of pitch fibers adhering to water is 0.1% by weight or less. After that, infusibilization treatment and carbonization treatment are performed according to a known method. For example, the infusibilizing treatment is carried out by heating the fibers to a temperature of 150 to 360 ° C. for 5 minutes to 1 in an oxidizing atmosphere such as oxygen, ozone, air, nitrogen oxides, and halogen sulfite gas.
It is carried out by heating for 0 hours. The carbonization is carried out by treating the fibers under an atmosphere of an inert gas such as nitrogen or argon at 100
It is carried out by heating to a temperature of 0 to 2500 ° C. for 0.5 minutes to 10 hours.

【0013】さらに黒鉛化処理を行う場合には、250
0〜3500℃の温度に1秒〜1時間加熱保持すればよ
い。また不融化、炭化あるいは黒鉛化処理の際、必要で
あれば収縮や変形等を防止する目的で、被処理体に若干
の荷重あるいは張力をかけておくこともできる。
When further graphitizing treatment is carried out, 250
The temperature may be kept at 0 to 3500 ° C. for 1 second to 1 hour. Further, during the infusibilizing, carbonizing or graphitizing treatment, if necessary, a slight load or tension may be applied to the object to be treated for the purpose of preventing shrinkage or deformation.

【0014】[0014]

【発明の効果】以上詳述したように、本発明ではシリコ
ーン油の水エマルジョンを付着させるという簡単な操作
で脆弱な繊維の取扱いを容易ならしめると同時に繊維相
互間の接着や融着あるいは繊維表面の損傷の発生が防止
されるので、性状の良好なピッチ系炭素繊維を連続フィ
ラメント状で工業的有利な条件の下で加熱処理を行うこ
とができるので、すぐれた性能を有するピッチ系炭素繊
維が廉価に得られるという利点もある。
As described in detail above, the present invention facilitates the handling of fragile fibers by the simple operation of adhering a water emulsion of silicone oil, and at the same time, adheres or fuses the fibers together or the fiber surface. Since the occurrence of damage to the pitch-based carbon fibers can be heat-treated under continuous industrially advantageous conditions in the form of continuous filaments of pitch-based carbon fibers, pitch-based carbon fibers having excellent performance are obtained. There is also an advantage that it can be obtained at a low price.

【0015】[0015]

【実施例】次に本発明を実施例により更に具体的に説明
するが、本発明はその要旨をこえない限り以下の実施例
に限定されるものではない。 (実施例1〜9)タール系の原料ピッチ(光学的異方性
100%のメソ相ピッチ)を紡糸口金温度330℃で溶
融紡糸し、得られた糸系10μmのピッチ繊維に、第1
表に示す集束剤を噴霧して付着させ集束した。次いで集
束繊維(トウ)を空気中に於いて80℃に30分間保持
して乾燥した。次いで150℃より350℃まで2時間
40分を要して昇温した後その温度に30分間保持して
不融化処理を行った。その後アルゴン中に於いて、室温
より1400℃までに2時間20分を要して昇温した後
その温度に1時間保持して炭化処理を行い炭素繊維を得
た。炭素繊維製造工程における糸の集束状態、不融化繊
維の性状、単糸の融着状態を観察し、また炭素繊維の引
張強度を測定し、その結果を第1表及び第2表に記載す
る。又、紡糸以降の工程については簡単な説明図を図1
として示す。
EXAMPLES Next, the present invention will be described more specifically by way of examples, but the present invention is not limited to the following examples unless it exceeds the gist. (Examples 1 to 9) Tar-based raw material pitch (mesophase pitch with 100% optical anisotropy) was melt-spun at a spinneret temperature of 330 ° C.
The sizing agent shown in the table was sprayed and adhered for focusing. The bundled fibers (tows) were then dried by holding them in air at 80 ° C. for 30 minutes. Next, the temperature was raised from 150 ° C. to 350 ° C. over 2 hours and 40 minutes, and then the temperature was maintained for 30 minutes for infusibilization treatment. Then, in argon, the temperature was raised from room temperature to 1400 ° C. over 2 hours and 20 minutes, and then the temperature was maintained for 1 hour to carry out carbonization treatment to obtain carbon fibers. In the carbon fiber manufacturing process, the bundled state of the yarn, the property of the infusibilized fiber, and the fused state of the single yarn were observed, and the tensile strength of the carbon fiber was measured. The results are shown in Tables 1 and 2. In addition, a simple explanatory drawing is shown in FIG.
As shown.

【0016】(比較例1〜7)実施例1において、集束
剤を使うことなく、又は集束剤添着量、エマルジョン濃
度あるいは集束剤種を変えて実施例1と同様に実施した
結果を第1表及び第2表に併記する。
(Comparative Examples 1 to 7) Table 1 shows the results obtained in Example 1 in the same manner as in Example 1 without using the sizing agent or by changing the sizing agent impregnation amount, emulsion concentration or sizing agent type. And Table 2 together.

【0017】[0017]

【表1】 [Table 1]

【0018】[0018]

【表2】 [Table 2]

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

【図1】本発明における炭素繊維の紡糸以降の工程に関
する説明図。
FIG. 1 is an explanatory diagram related to the steps after spinning of carbon fiber in the present invention.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 原料ピッチを溶融紡糸して得られたピッ
チ繊維を集束後、不融化処理、さらに必要に応じて黒鉛
化処理を行うことによりピッチ系炭素繊維を製造する方
法に於いて、集束の際又は集束前のピッチ繊維に、集束
剤としてシリコーン油の濃度が0.1〜35重量%であ
るシリコーン油の水エマルジョンを付着させた後、更に
不融化炉の直前に設けた乾燥炉か不融化炉の最初の過程
において50〜100℃に5分〜2時間保持して乾燥す
ることを特徴とするピッチ系炭素繊維の製造方法。
1. A method for producing pitch-based carbon fibers by concentrating pitch fibers obtained by melt-spinning raw material pitch, and then subjecting to infusibilization treatment and, if necessary, graphitization treatment, In the drying furnace provided immediately before the infusibilizing furnace after adhering a water emulsion of silicone oil having a silicone oil concentration of 0.1 to 35% by weight as a sizing agent to the pitch fiber before or before sizing. A method for producing a pitch-based carbon fiber, which is characterized by holding at 50 to 100 ° C. for 5 minutes to 2 hours and drying in the first step of the infusibilizing furnace.
【請求項2】 集束剤を繊維に対して2〜14重量%付
着させることを特徴とする特許請求の範囲第1項記載の
方法。
2. The method according to claim 1, wherein the sizing agent is applied in an amount of 2 to 14% by weight based on the fiber.
JP7247680A 1995-09-26 1995-09-26 Manufacturing method of pitch-based carbon fiber Expired - Lifetime JP2708055B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7247680A JP2708055B2 (en) 1995-09-26 1995-09-26 Manufacturing method of pitch-based carbon fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7247680A JP2708055B2 (en) 1995-09-26 1995-09-26 Manufacturing method of pitch-based carbon fiber

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP59190404A Division JPH06102852B2 (en) 1984-09-11 1984-09-11 Pitch-based carbon fiber manufacturing method

Publications (2)

Publication Number Publication Date
JPH0860448A true JPH0860448A (en) 1996-03-05
JP2708055B2 JP2708055B2 (en) 1998-02-04

Family

ID=17167059

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Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2708055B2 (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58208465A (en) * 1982-05-26 1983-12-05 東レ株式会社 Raw yarn oil agent for producing carbon fiber
JPS60173121A (en) * 1984-02-16 1985-09-06 Toa Nenryo Kogyo Kk Production of carbon yarn and graphite yarn

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58208465A (en) * 1982-05-26 1983-12-05 東レ株式会社 Raw yarn oil agent for producing carbon fiber
JPS60173121A (en) * 1984-02-16 1985-09-06 Toa Nenryo Kogyo Kk Production of carbon yarn and graphite yarn

Also Published As

Publication number Publication date
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