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JPH0823089B2 - Method for producing pitch-based carbon fiber - Google Patents
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JPH0823089B2 - Method for producing pitch-based carbon fiber - Google Patents

Method for producing pitch-based carbon fiber

Info

Publication number
JPH0823089B2
JPH0823089B2 JP4137988A JP4137988A JPH0823089B2 JP H0823089 B2 JPH0823089 B2 JP H0823089B2 JP 4137988 A JP4137988 A JP 4137988A JP 4137988 A JP4137988 A JP 4137988A JP H0823089 B2 JPH0823089 B2 JP H0823089B2
Authority
JP
Japan
Prior art keywords
pitch
treatment
fibers
aliphatic carboxylic
carboxylic acid
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
JP4137988A
Other languages
Japanese (ja)
Other versions
JPH01221519A (en
Inventor
耕二 末村
宏規 武山
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 JP4137988A priority Critical patent/JPH0823089B2/en
Publication of JPH01221519A publication Critical patent/JPH01221519A/en
Publication of JPH0823089B2 publication Critical patent/JPH0823089B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
  • Inorganic Fibers (AREA)
  • Chemical Treatment Of Fibers During Manufacturing Processes (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 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。
TECHNICAL FIELD The present invention relates to a method for producing carbon fiber from pitches such as coal pitch, petroleum pitch, and polymer fired pitch. The present invention relates to a method for obtaining a high-quality carbon fiber which is easy to handle and is free from adhesion or fusion between fibers.

〔従来の技術〕[Conventional technology]

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
な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
ーラへの捲きつき、糸切れ等を起こしやすい。更に不融
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に損傷を生じ易いという難
点があった。
Pitch-based carbon fibers are usually produced by melt-spinning raw material pitch and subjecting the obtained pitch fibers to infusibilization treatment and carbonization treatment. Pitch-based carbon fibers have the advantage of being industrially advantageous in high yield compared to polyacrylonitrile-based carbon fibers, but pitch fibers are extremely fragile, making them difficult to handle by infusibilizing treatment or carbonization treatment. In these steps, fiber fluffing, winding around the guide roller, yarn breakage, etc. are likely to occur. Further, there is a problem that the pitch fibers are adhered or fused to each other during the infusibilizing treatment and the carbonizing treatment, and the obtained carbon fibers are easily damaged.

そこで、かかるピッチ系炭素繊維に特有の難点を解消
して高品質のピッチ系炭素繊維を安定的に製造し得る方
法について種々検討し、処理剤としてシリコーンオイル
水エマルジョンを用いる方法(特開昭61−70017号公
報)について提案したが、この処理剤では紡糸集束工程
における繊維の毛羽立ち、ガイドローラーへの捲きつ
き、糸切れ等の問題点は解決できたが、酸化性雰囲気
下、約100℃〜約400℃程度の加熱帯域で行なう不融化処
理あるいはかかる不融化処理に後続する不活性雰囲気下
で少なくとも400℃以上で加熱処理する炭化処理におい
て繊維相互間の融着や接着を十分に解消するには未だ改
善する余地を残していた。
Therefore, various studies have been made on a method capable of stably producing a high-quality pitch-based carbon fiber by solving the problems inherent in the pitch-based carbon fiber, and a method using a silicone oil / water emulsion as a treating agent (JP-A-61). No. 70017), this treatment agent has solved the problems of fiber fluffing, winding around guide rollers, yarn breakage, etc. in the spin focusing process, but at about 100 ° C. in an oxidizing atmosphere. In order to sufficiently eliminate fusion and adhesion between fibers in the infusibilizing treatment performed in a heating zone of about 400 ° C or in the carbonizing treatment following the infusibilizing treatment at a temperature of at least 400 ° C or more in an inert atmosphere. Still had room for improvement.

このような融着あるいは接着という現象の原因は、不
融化処理あるいは炭化処理等の加熱処理時に、処理剤に
含有される界面活性剤の一部が分解あるいはタール化す
ることであることが判明した。
It has been found that the cause of such a phenomenon of fusion or adhesion is that a part of the surfactant contained in the treating agent is decomposed or tarified during the heat treatment such as the infusibilizing treatment or the carbonizing treatment. .

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

そこで本発明者等はかかる界面活性剤の繊維に対する
影響を調査・検討した結果、種々の界面活性剤のうち、
脂肪族カルボン酸アルカノールアミドあるいは脂肪族カ
ルボン酸アミン塩は不融化処理あるいは炭化処理等の加
熱処理等に繊維間の融着や膠着を発生させることがない
ことを見出した。しかし、脂肪族カルボン酸アルカノー
ルアミドまたは/および脂肪族カルボン酸アミド塩を用
いて得られたシリコーン油の水エマルジョンを繊維に付
着して集束させた場合、集束性が十分でなく、工程を通
過するものの繊維の毛羽立ち、ガイドローラーへの捲き
つけ、糸切れ等の問題点が若干残り、かつ集束剤を付着
した繊維を数日乃至1週間程度保存したときこれらの問
題点がより顕著になるという難点があった。
Therefore, the present inventors have investigated and studied the effect of such a surfactant on fibers, and as a result, among various surfactants,
It has been found that the aliphatic carboxylic acid alkanolamide or the aliphatic carboxylic acid amine salt does not cause fusion or sticking between fibers during heat treatment such as infusibilization treatment or carbonization treatment. However, when an aqueous emulsion of a silicone oil obtained by using an aliphatic carboxylic acid alkanolamide or / and an aliphatic carboxylic acid amide salt is attached to fibers to be bundled, the sizing property is not sufficient, and the process passes. However, some problems such as fluffing of fibers, wrapping around guide rollers, and thread breakage remain, and these problems become more noticeable when the fibers to which the sizing agent is attached are stored for several days to one week. was there.

一方、従来集束剤の界面活性剤としてよく用いられて
いるポリオキシエチレンアルキルエーテルを用いたシリ
コーン油水エマルジョンは集束性にすぐれ繊維の毛羽立
ち、ガイドローラーへの巻きつき、糸切れ等が非常に少
く、かつ集束剤を付着した繊維を1週間程度保存したと
きの性能劣化も少ないが、不融化処理あるいは炭化処理
での熱処理時に繊維間の融着や膠着を発生させるという
問題があった。
On the other hand, a silicone oil / water emulsion using polyoxyethylene alkyl ether, which is often used as a surfactant for conventional sizing agents, has excellent sizing properties, and fiber fluffing, winding around guide rollers, and yarn breakage are very small. Moreover, although the performance deterioration of the fiber to which the sizing agent is attached is stored for about one week, there is a problem that fusion or gluing of the fiber occurs during heat treatment in the infusibilizing treatment or the carbonizing treatment.

〔問題点を解決するための手段〕[Means for solving problems]

そこで本発明者等はこれらの問題点を解決するため鋭
意検討を重ねた結果、界面活性剤が複数の成分からな
り、少くとも一成分がポリオキシエチレンアルキルエー
テルであり、他の成分が脂肪族カルボン酸アルカノール
アミドまたは/および脂肪族カルボン酸アミン塩である
シリコーン油水エマルジョンを用いることにより上記問
題点が解決されることを見出し、本発明に到達した。
Therefore, the present inventors have conducted extensive studies to solve these problems, and as a result, the surfactant is composed of a plurality of components, at least one component is a polyoxyethylene alkyl ether, the other component is an aliphatic The inventors have found that the above problems can be solved by using a silicone oil-water emulsion that is a carboxylic acid alkanolamide or / and an aliphatic carboxylic acid amine salt, and have reached the present invention.

すなわち、本発明の要旨は、紡糸ピッチを気相中に溶
融紡糸して得られたピッチ繊維をシリコーン油の水エマ
ルジョンを用いて集束後、不融化処理、炭化処理、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おいて、水エマルジョン中の界
面活性剤が複数の成分からなり、少なくとも一成分がポ
リオキシエチレンアルキルエーテルであり、他の成分が
脂肪族カルボン酸アルカノールアミドまたは/および脂
肪族カルボン酸アミン塩であることを特徴とするピッチ
系炭素繊維の製造法に存する。
That is, the gist of the present invention is that after pitch fibers obtained by melt-spinning a spinning pitch in a gas phase are bundled by using a water emulsion of silicone oil, infusibilization treatment, carbonization treatment, and further graphitization as necessary. In the method for producing a pitch-based carbon fiber by performing treatment, the surfactant in the water emulsion is composed of a plurality of components, at least one component is polyoxyethylene alkyl ether, and the other component is an aliphatic carboxylic acid alkanol. An amide or / and an amine salt of an aliphatic carboxylic acid, which is a method for producing a pitch-based carbon fiber.

以下本発明を詳細に説明するに、本発明に用いられる
紡糸ピッチとしては、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, as the spinning pitch used in the present invention, coal tar pitch, coal pitch such as coal liquefaction, atmospheric distillation residual oil of crude oil, vacuum distillation residual oil, or heat-treated product thereof. Examples thereof include petroleum-based pitches such as heat-treated products of thermal decomposition by-product tar of naphtha, and polymer calcined pitches obtained by carbonization of synthetic resins and natural resins.

紡糸ピッチの溶融紡糸は通常の合成繊維の乾式法溶融
紡糸と同様に行なうことができ、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250〜350℃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。
The melt spinning of the spinning pitch can be performed in the same manner as the dry method melt spinning of synthetic fibers, and there is no particular limitation, and the method of extruding the melted spinning pitch from the downward spinneret into the gas phase and cooling and solidifying is adopted. . 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 kind of the raw material pitch and is determined by taking into consideration the melt viscosity suitable for spinning, but normally the range of 250 to 350 ° C is suitable. It is effective to stabilize the spinning state by providing a heat insulation tube below the spinneret.

本発明においては、上記の方法で紡糸されたピッチ繊
維に対して付着使用する、シリコーン油を界面活性剤に
より水中に分散した処理剤が用いられるが、界面活性剤
は複数の成分から成り、少なくとも一成分がポリオキシ
エチレンアルキルエーテルであり、他の成分が脂肪族カ
ルボン酸アルカノールアミドまたは/および脂肪族カル
ボン酸アミン塩から成るものを用いるのが重要である。
In the present invention, a treating agent in which silicone oil is dispersed in water by a surfactant, which is used by attaching to pitch fibers spun by the above method, is used. It is important to use those in which one component is a polyoxyethylene alkyl ether and the other component consists of an aliphatic carboxylic acid alkanolamide or / and an aliphatic carboxylic acid amine salt.

かかる界面活性剤の成分であるポリオキシエチレンア
ルキルエーテルとしてはラウリル、セチル、オレイルお
よび牛脂肪アルコール等の動植物系アルコール、オキソ
アルコール、ガーベットアルコール等の合成アルコー
ル、樹脂アルコールなどの脂肪族アルコールに酸化エチ
レンを付加重合させたものが挙げられ、一般式 RO(CH2CH2O)nH (ここでRはC8〜C20の置換されていてもよいアルキル
基又はアルケニル基、nは1〜20の整数)で示される。
Examples of the polyoxyethylene alkyl ether which is a component of such a surfactant include animal and plant alcohols such as lauryl, cetyl, oleyl and beef fatty alcohol, synthetic alcohols such as oxo alcohol and gerbet alcohol, and aliphatic alcohols such as resin alcohol. Examples thereof include those obtained by addition-polymerizing ethylene, and are represented by the general formula RO (CH 2 CH 2 O) n H (wherein R is a C 8 to C 20 optionally substituted alkyl group or alkenyl group, and n is 1 to 1). 20 integer).

一方、脂肪族カルボン酸アルカノールアミドとしては
カプリン酸、ラウリン酸、ヤシ脂肪酸、ミリスチン酸、
ステアリン酸、オレイン酸等の脂肪族カルボン酸とモノ
エタノールアミン、ジエタノールアミン、モノイソプロ
パノールアミン、ジイソプロパノールアミンなどの縮合
生成物が挙げられ、一般式 R1CONH(R2O)nH 又は (ただしR1はC8〜C22の置換されていてもよいアルキル
基又はアルケニル基を、R2、R3はC1〜C4の置換されてい
てもよいアルキレン基を、nおよびmは1〜20の整数を
示す。)で示される。
On the other hand, as the aliphatic carboxylic acid alkanolamide, capric acid, lauric acid, coconut fatty acid, myristic acid,
Condensation products such as stearic acid and aliphatic carboxylic acids such as oleic acid and monoethanolamine, diethanolamine, monoisopropanolamine, diisopropanolamine and the like can be mentioned, and general formula R 1 CONH (R 2 O) n H or (However, R 1 is a C 8 to C 22 optionally substituted alkyl group or alkenyl group, R 2 and R 3 are C 1 to C 4 optionally substituted alkylene groups, and n and m are It represents an integer of 1 to 20).

市販のアルカノールアミドには製法によりアルカノー
ルアミンと脂肪族カルボン酸の比率が2:1型のものおよ
び1:1型のものがあるがそのどちらも用いることができ
る。
Commercially available alkanolamides include those having a ratio of alkanolamine to aliphatic carboxylic acid of 2: 1 type and those of 1: 1 type depending on the production method, and either of them can be used.

脂肪族カルボン酸アミン塩としては一般式 (R1はC6〜C20の置換されていてもよいアルキル基、ア
ルケニル基、R2、R3、R4はそれぞれ置換されていてもよ
いC1〜C10のアルキル基、アルケニル基、ヒドロキシア
ルキル基、ポリオキシアルキル基又は水素原子を表わ
す)で表わされる脂肪族カルボン酸と1〜3級アミンの
塩で示される。具体的には脂肪族カルボン酸としてはオ
クタン酸、デカン酸、ラウリル酸、パルミチン酸、ステ
アリン酸等が、アミンとしてはメチルアミン、ジメチル
アミン、トリメチルアミン、エチルアミン、ジエチルア
ミン、トリエチルアミン、トリプロピルアミン、モノエ
タノールアミン、ジエタノールアミン、トリエタノール
アミン、モルホリン、ジメチルアミノプロピルアミン、
モノイソプロピルアミン、ジイソプロピルアミン、トリ
イソプロピルアミン、ブチルジエタノールアミン、ジブ
チルエタノールアミン、アミノエチルエタノールアミ
ン、ペンチルジエタノールアミン等が挙げられる。
The aliphatic carboxylic acid amine salt has a general formula (R 1 is a C 6 to C 20 optionally substituted alkyl group, an alkenyl group, R 2 , R 3 , R 4 are each optionally substituted C 1 to C 10 alkyl group, an alkenyl group, It is represented by a salt of an aliphatic carboxylic acid represented by a hydroxyalkyl group, a polyoxyalkyl group or a hydrogen atom) and a primary to tertiary amine. Specifically, the aliphatic carboxylic acids include octanoic acid, decanoic acid, lauric acid, palmitic acid, stearic acid, etc., and the amines include methylamine, dimethylamine, trimethylamine, ethylamine, diethylamine, triethylamine, tripropylamine, monoethanol. Amine, diethanolamine, triethanolamine, morpholine, dimethylaminopropylamine,
Examples include monoisopropylamine, diisopropylamine, triisopropylamine, butyldiethanolamine, dibutylethanolamine, aminoethylethanolamine, pentyldiethanolamine and the like.

シリコーン油としてはジメチルポリシロキサン、メチ
ルフェニルポリシロキサンあるいは種々の変性ポリシロ
キサン等が挙げられ、好しくは粘度(25℃における)が
0.65〜1,000,000cst、更に好ましくは1〜1000cstのも
のを使用するのがよい。またシリコーン油は2種以上の
混合物を用いてもよい。
Examples of the silicone oil include dimethylpolysiloxane, methylphenylpolysiloxane and various modified polysiloxanes, and preferably the viscosity (at 25 ° C) is
0.65 to 1,000,000 cst, more preferably 1 to 1000 cst, is preferably used. Moreover, you may use the mixture of 2 or more types of silicone oil.

界面活性剤の使用量はシリコーン油に対して総量で1w
t%〜25wt%が好ましい。1wt%未満ではシリコーン油の
安定な水エマルジョンが得られず、25wt%より多いと不
融化あるいは炭化後の繊維の性状に悪影響を及ぼすこと
がある。また界面活性剤の内、ポリオキシエチレンアル
キルエーテルの量は好しくはシリコーン油に対して0.1w
t%〜6wt%程度、更に好しくは0.2wt%〜2wt%程度であ
る。少なすぎると集束性が十分でなく、多すぎると不融
化あるいは炭化後の繊維性状に悪影響を及ぼすことがあ
る。
The total amount of surfactant used for silicone oil is 1w
t% to 25 wt% is preferable. If it is less than 1 wt%, a stable water emulsion of silicone oil cannot be obtained, and if it exceeds 25 wt%, the properties of the fiber after infusibilization or carbonization may be adversely affected. Of the surfactants, the amount of polyoxyethylene alkyl ether is preferably 0.1 w relative to silicone oil.
t% to 6 wt%, more preferably 0.2 wt% to 2 wt%. If the amount is too small, the bundling property is not sufficient, and if the amount is too large, the fiber properties after infusibilization or carbonization may be adversely affected.

更に、脂肪族カルボン酸アルカノールアミドまたは/
および脂肪族カルボン酸アミン塩はシリコーン油に対し
て0.1wt%〜24wt%程度とするのが好ましい。
Furthermore, aliphatic carboxylic acid alkanolamide or /
Also, the amine salt of aliphatic carboxylic acid is preferably about 0.1 wt% to 24 wt% with respect to the silicone oil.

また、種々の目的のために本発明の効果を害さない範
囲で従来公知の乳化剤、静電気防止剤、防錆剤、抗菌剤
等を含有することは可能である。
Further, for various purposes, it is possible to contain conventionally known emulsifiers, antistatic agents, rust preventives, antibacterial agents, etc. within a range that does not impair the effects of the present invention.

以上の組成より成る処理剤は通常オイル分(シリコー
ン油と界面活性剤の総量)が0.1wt%〜30wt%の水エマ
ルジョンとして使用するが、ピッチ繊維に対する添着量
はオイル分として0.02wt%〜15wt%、好ましくは0.2wt
%〜5wt%とするのがよい。0.02wt%未満では集束性が
得られず、15wt%を超えると不融化あるいは炭化後の繊
維性状に悪影響を及ぼすことがある。
The treating agent having the above composition is usually used as a water emulsion with an oil content (total amount of silicone oil and surfactant) of 0.1 wt% to 30 wt%, but the amount of impregnation on pitch fibers is 0.02 wt% to 15 wt%. %, Preferably 0.2 wt
% To 5 wt% is recommended. If it is less than 0.02% by weight, the bundling property cannot be obtained, and if it exceeds 15% by weight, the fiber properties after infusibilization or carbonization may be adversely affected.

処理剤を繊維に添着する方法としては、紡糸口金を出
た走行糸にスプレーにより吹付ける方法、ローラーに付
けて接触させる方法、カラス口に付けて接触させる方法
等より適宜選択することができる。
The method of attaching the treatment agent to the fiber can be appropriately selected from a method of spraying the running yarn coming out of the spinneret by spraying, a method of contacting with a roller and a method of contacting with a crow's mouth, and the like.

処理剤が付与され、集束されたピッチ繊維は周知の方
法に従って不融化処理及び炭化処理が行なわれる。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、150〜3
60℃の温度に5分〜10時間加熱することによって行われ
る。
The pitch fiber bundled with the treatment agent is subjected to infusibilization treatment and carbonization treatment according to known methods. For example, the infusibilizing treatment is carried out by treating the fibers in an oxidizing atmosphere such as oxygen, ozone, air, nitrogen oxide, halogen, and sulfurous acid gas at 150 to 3
It is carried out by heating to a temperature of 60 ° C. for 5 minutes to 10 hours.

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、400〜2000℃の温度に0.5〜10時間加熱することに
よって行われる。
The carbonization treatment is carried out by heating the fibers at a temperature of 400 to 2000 ° C. for 0.5 to 10 hours in an atmosphere of an inert gas such as nitrogen or argon.

さらに黒鉛化処理を行う場合には2000〜3500℃の温度
に1秒〜1時間程度加熱保持すればよい。
Further, when the graphitization treatment is performed, the temperature may be kept at 2000 to 3500 ° C. for about 1 second to 1 hour.

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張力をか
けておくこともできる。
In addition, during infusibilization, carbonization or graphitization, it is also possible to apply tension to the object to be treated for the purpose of preventing shrinkage, deformation or the like.

このようにして得られた炭素繊維又は黒鉛化繊維は必
要により表面処理又は/およびサイジング処理した後、
それぞれの用途に用いられる。
The carbon fiber or the graphitized fiber thus obtained is optionally surface-treated or / and sized,
Used for each purpose.

(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。
(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.

実施例1〜4 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340℃で気相中へ溶融紡糸し、
得られた糸系10μm、1000フィラメントのピッチ繊維
に、第1表に示す処理剤をオイリングガイドを用いて付
着させ集束した。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
処理を行なった。その後アルゴン中において、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ない炭素繊維を得た。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た。その結果を第1表に記
載する(%はwt%を示す)。
Examples 1 to 4 Tar-based raw material pitch (mesophase pitch with 100% optical anisotropy) was melt-spun into the gas phase at a spinneret temperature of 340 ° C.,
The treating agents shown in Table 1 were attached to the obtained pitch fiber of 10 μm and 1000 filament pitch fibers by using an oiling guide and then bundled. Then, 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, from room temperature
It took 2 hours and 20 minutes to reach 1400 ° C., 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 infusible fiber, and the fused state of the single yarn were observed. The results are shown in Table 1 (% indicates wt%).

比較例1〜4 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表に示す。
Comparative Examples 1 to 4 Table 1 shows the results of the same procedure as in Example 1 except that the sizing agent type was changed.

第1表の結果からも、本発明に係る処理剤の優れた諸
性能は明らかである。
The excellent performances of the treating agent according to the present invention are apparent from the results shown in Table 1.

〔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を特定
の界面活性剤で水中に分散してなる炭素繊維用処理剤を
用いることにより、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が防止
され、性状の良好なピッチ系炭素繊維を連続フィラメン
ト状で工業的に有利な条件下で製造できる。
[Effects of the Invention] As described in detail above, in the present invention, by using a treatment agent for carbon fibers obtained by dispersing silicone oil in water with a specific surfactant, it is possible to handle brittle fibers with a simple operation. Pitch-based carbon fibers having good properties can be produced in the form of continuous filaments under industrially advantageous conditions while facilitating the easiness and preventing the mutual adhesion and fusion of the fibers.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 D06M 13/419 15/643 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display location D06M 13/419 15/643

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】原料ピッチを気相中に溶融紡糸して得られ
たピッチ繊維をシリコーン油の水エマルジョンを用いて
集束後、不融化処理、炭化処理、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
方法において、水エマルジョン中の界面活性剤が複数の
成分からなり、少なくとも一成分がポリオキシエチレン
アルキルエーテルであり、他の成分が脂肪族カルボン酸
アルカノールアミドまたは/および脂肪族カルボン酸ア
ミン塩であることを特徴とするピッチ系炭素繊維の製造
方法。
1. A pitch fiber obtained by melt-spinning a raw material pitch in a gas phase is bundled with a water emulsion of silicone oil, and then subjected to infusibilization treatment, carbonization treatment and, if necessary, graphitization treatment. In the method for producing a pitch-based carbon fiber according to the above, the surfactant in the water emulsion is composed of a plurality of components, at least one component is a polyoxyethylene alkyl ether, and the other component is an aliphatic carboxylic acid alkanolamide or / And a method for producing a pitch-based carbon fiber, which is an aliphatic carboxylic acid amine salt.
JP4137988A 1988-02-24 1988-02-24 Method for producing pitch-based carbon fiber Expired - Lifetime JPH0823089B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4137988A JPH0823089B2 (en) 1988-02-24 1988-02-24 Method for producing pitch-based carbon fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4137988A JPH0823089B2 (en) 1988-02-24 1988-02-24 Method for producing pitch-based carbon fiber

Publications (2)

Publication Number Publication Date
JPH01221519A JPH01221519A (en) 1989-09-05
JPH0823089B2 true JPH0823089B2 (en) 1996-03-06

Family

ID=12606765

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4137988A Expired - Lifetime JPH0823089B2 (en) 1988-02-24 1988-02-24 Method for producing pitch-based carbon fiber

Country Status (1)

Country Link
JP (1) JPH0823089B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0657889B2 (en) * 1988-02-24 1994-08-03 竹本油脂株式会社 Oil agent for carbon fiber production
JP3481342B2 (en) * 1995-03-17 2003-12-22 松本油脂製薬株式会社 Precursor oil composition for carbon fiber

Also Published As

Publication number Publication date
JPH01221519A (en) 1989-09-05

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