JPH05214613A - Production of mesophase pitch-based carbon fiber - Google Patents

Production of mesophase pitch-based carbon fiber

Info

Publication number
JPH05214613A
JPH05214613A JP20176892A JP20176892A JPH05214613A JP H05214613 A JPH05214613 A JP H05214613A JP 20176892 A JP20176892 A JP 20176892A JP 20176892 A JP20176892 A JP 20176892A JP H05214613 A JPH05214613 A JP H05214613A
Authority
JP
Japan
Prior art keywords
fiber
pitch
mesophase pitch
solvent
carbon fiber
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP20176892A
Other languages
Japanese (ja)
Inventor
Hisafumi Kawamura
寿文 河村
Takashi Maeda
嵩志 前田
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.)
PETOCA KK
Original Assignee
PETOCA KK
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 PETOCA KK filed Critical PETOCA KK
Priority to JP20176892A priority Critical patent/JPH05214613A/en
Publication of JPH05214613A publication Critical patent/JPH05214613A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain the subject mesophase pitch-based carbon fiber, useful for obtaining infusibilized fiber, having retained molecular orientation possessed by the pitch fiber itself and improved in physical properties by oxidatively polymerizing mesophase pitch fiber in the liquid phase at a low temperature. CONSTITUTION:The objective method for producing mesophase pitch-based carbon fiber is to (1) melt spin mesophase pitch according to a conventional method, provide pitch fiber, oxidatively polymerize the fiber in the liquid phase in a solvent in the presence of an acidic catalyst and a cross-linking agent and infusibilize the fiber. In the method, (2) an acidic solvent such as a carboxylic acid is used as the solvent and (3) the oxidatively polymerizing conditions are 90-150 deg.C and 0.1-10hr. The mixing ratios of the cross-linking agent and acidic catalyst to the pitch fiber are respectively 0.0001-0.05mol and 0.0001-0.05mol based on 1g pitch fiber.

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、メソフェーズピッチ系
炭素繊維の改良された製造方法に関する。より詳細に
は、本発明の方法は、メソフェーズピッチ繊維を低温で
液相酸化・重合することにより、不融化繊維を得るもの
であり、ピッチ繊維自体の保有する分子配向が保持され
ていて、物性の向上したメソフェーズピッチ系炭素繊維
を提供するものである。
FIELD OF THE INVENTION The present invention relates to an improved process for producing mesophase pitch carbon fibers. More specifically, the method of the present invention is to obtain infusible fibers by liquid-phase oxidation / polymerization of mesophase pitch fibers at a low temperature, the molecular orientation of the pitch fibers themselves is maintained, and To provide an improved mesophase pitch carbon fiber.

【0002】[0002]

【従来の技術】従来、メソフェーズピッチを紡糸してメ
ソフェーズピッチ繊維を製造し、それを空気中で200
〜400℃程度の高温で酸化・重合することにより、得
られる不融化繊維は、繊維内部にまで酸素が侵入し、酸
化によってピッチ分子の配向性が低下しているために、
後段の炭化過程における結晶成長が阻害され、かつ導入
された酸素原子の脱離に伴って構造欠陥が生じることか
ら、高物性の炭素繊維を得ることが難しかった。
2. Description of the Related Art Conventionally, mesophase pitch fibers are spun to produce mesophase pitch fibers, and the mesophase pitch fibers are produced in air for 200
By oxidizing and polymerizing at a high temperature of about 400 ° C., the infusible fiber obtained has oxygen penetrating into the inside of the fiber, and the orientation property of the pitch molecule is lowered by the oxidation.
It was difficult to obtain a carbon fiber having high physical properties because the crystal growth in the latter carbonization process is hindered and a structural defect occurs due to the desorption of the introduced oxygen atom.

【0003】[0003]

【発明が解決しようとする課題】上記のように、従来法
の気相酸化による不融化繊維の製造法では、ピッチ分子
の配向性が低下するために、後段の炭化過程における結
晶成長が阻害されるなどの理由により充分に結晶構造を
成長させることが難しく、高物性のメソフェーズピッチ
系炭素繊維を得ることが難しいものであった。
As described above, in the conventional method for producing infusibilized fiber by vapor phase oxidation, the orientation of pitch molecules is lowered, so that the crystal growth in the subsequent carbonization process is hindered. Therefore, it was difficult to grow a crystal structure sufficiently, and it was difficult to obtain a mesophase pitch carbon fiber having high physical properties.

【0004】本発明者らは、上記問題点を種々検討した
結果、メソフェーズピッチから得られたメソフェーズピ
ッチ繊維を、比較的低温下で液相酸化・重合して不融化
することにより、不融化による分子配向の乱れが抑制さ
れて、メソフェーズピッチ繊維形成時の配向を保持した
まま、不融化繊維を形成することができ、その結果、予
期せずして物性、特に引張強度の向上したメソフェーズ
ピッチ系炭素繊維が得られることを見出し、本発明を完
成するに至った。
As a result of various studies on the above-mentioned problems, the present inventors have conducted insolubilization by mesophase pitch fibers obtained from mesophase pitch being infusibilized by liquid phase oxidation / polymerization at a relatively low temperature. The disorder of the molecular orientation is suppressed, and the infusibilized fiber can be formed while maintaining the orientation during the formation of the mesophase pitch fiber. As a result, the mesophase pitch system with unexpectedly improved physical properties, especially tensile strength, can be formed. The inventors have found that carbon fibers can be obtained, and completed the present invention.

【0005】[0005]

【課題を解決するための手段】すなわち、本発明は: メソフェーズピッチを常法に従って溶融紡糸してピ
ッチ繊維とした後、該ピッチ繊維を酸触媒と架橋剤の存
在下で溶媒中で液相酸化・重合することにより不融化す
ることを特徴とする、メソフェーズピッチ系炭素繊維の
製造方法であり、また
Means for Solving the Problems The present invention is as follows: Melt-spinning mesophase pitch into pitch fibers by a conventional method, and then subjecting the pitch fibers to liquid-phase oxidation in a solvent in the presence of an acid catalyst and a crosslinking agent. A method for producing a mesophase pitch carbon fiber, which is characterized by being infusibilized by polymerizing,

【0006】 溶媒としてカルボン酸等の酸性溶媒を
使用する点にも特徴を有し、さらに 酸化・重合条件が90〜150℃で0.1〜10時
間であり、かつピッチ繊維に対する架橋剤及び酸触媒の
混合比が、夫々ピッチ繊維1g当たり0.0001〜
0.05モル及び0.0001〜0.05モルである点
にも特徴を有する。
It is also characterized in that an acidic solvent such as carboxylic acid is used as a solvent, and the oxidation / polymerization conditions are 90 to 150 ° C. for 0.1 to 10 hours, and the crosslinking agent and the acid for the pitch fiber are The mixing ratio of the catalyst is 0.0001 to 1 g of pitch fiber, respectively.
It is also characterized in that it is 0.05 mol and 0.0001 to 0.05 mol.

【0007】以下、本発明を詳細に述べる。本発明にお
いて、高物性のメソフェーズピッチ系炭素繊維を製造す
るには、(イ)メソフェーズピッチを常法に従って紡糸
してピッチ繊維を製造し、(ロ)該ピッチ繊維を酸触媒
と架橋剤の存在下で比較的低温で溶媒中で酸化・重合す
ることが必要である。
The present invention will be described in detail below. In the present invention, to produce mesophase pitch-based carbon fiber having high physical properties, (a) the mesophase pitch is spun according to a conventional method to produce pitch fiber, and (b) the pitch fiber is present in the presence of an acid catalyst and a crosslinking agent. It is necessary to oxidize and polymerize in a solvent at a relatively low temperature.

【0008】このような方法の採用により、不融化によ
る分子配向の乱れが抑制されて、ピッチ繊維形成時の配
向を保持したまま、ピッチ繊維の表層を酸化・重合して
不融化繊維を形成することができ、高物性のメソフェー
ズピッチ系炭素繊維を製造できるのである。
By adopting such a method, the disorder of the molecular orientation due to infusibilization is suppressed, and the surface layer of the pitch fiber is oxidized and polymerized to form the infusibilized fiber while maintaining the orientation at the time of pitch fiber formation. Therefore, the mesophase pitch carbon fiber having high physical properties can be produced.

【0009】本発明の方法に用いる、メソフェーズピッ
チは、石油ピッチ、石炭ピッチから常法に従って濾過、
精製、蒸留、水添、接触分解などの処理工程を適宜選択
して製造される。なお、繊維物性の点では、メソフェー
ズ含有率が約70%以上のメソフェーズピッチを用いる
ことが好ましい。
The mesophase pitch used in the method of the present invention includes petroleum pitch and coal pitch, which are filtered by a conventional method.
It is produced by appropriately selecting treatment steps such as purification, distillation, hydrogenation and catalytic decomposition. From the viewpoint of fiber properties, it is preferable to use mesophase pitch having a mesophase content of about 70% or more.

【0010】メソフェーズピッチ繊維の製造は、メソフ
ェーズピッチを繊維状に紡糸できるなら公知の紡糸方法
を採用できる。
The mesophase pitch fiber can be produced by a known spinning method as long as the mesophase pitch can be spun into a fibrous state.

【0011】メソフェーズピッチ繊維の液相酸化・重合
による不融化処理は、酸触媒と架橋剤の存在下で溶媒中
で比較的低温の調整された条件下で液相酸化・重合させ
ることが肝要である。
The infusibilization treatment of liquid phase oxidation / polymerization of mesophase pitch fibers requires that liquid phase oxidation / polymerization be performed under controlled conditions at a relatively low temperature in a solvent in the presence of an acid catalyst and a crosslinking agent. is there.

【0012】本発明におけるピッチ繊維の不融化のため
の酸化・重合反応の機構は、基本的にフェノール樹脂の
合成の場合と同様であると考えられる。
The mechanism of the oxidation / polymerization reaction for infusibilizing the pitch fiber in the present invention is considered to be basically the same as in the case of synthesizing a phenol resin.

【0013】本発明に使用する架橋剤としては、反応系
内で単量体のホルムアルデヒドを生成するものであれば
如何なる形態のものでも良く、市販の各種濃度のホルマ
リン、パラホルムアルデヒド、トリオキサンのようなア
ルデヒド類やヒドロキシメチル基を有する化合物を使用
できるが、触媒濃度を低下させず、低価格で入手できる
パラホルムアルデヒドの使用が好ましい。また、ガス状
のホルムアルデヒドを反応系に吹き込み仕込むこともで
きる。
The cross-linking agent used in the present invention may be in any form as long as it forms a monomer formaldehyde in the reaction system, such as various commercially available concentrations of formalin, paraformaldehyde and trioxane. Aldehydes and compounds having a hydroxymethyl group can be used, but it is preferable to use paraformaldehyde, which does not lower the catalyst concentration and can be obtained at a low price. Also, gaseous formaldehyde can be charged into the reaction system.

【0014】本発明に使用する酸触媒としては、溶媒に
可溶な酸触媒であれば特に制限されないが、例えば硫
酸、硝酸、塩酸、リン酸などの無機強酸;パラトルエン
スルホン酸などの有機強酸;三フッ化ホウ素、塩化アル
ミニウムなどのルイス酸などを挙げることができるが、
パラトルエンスルホン酸などの有機強酸の使用が触媒活
性、取り扱い性等の点で好ましい。
The acid catalyst used in the present invention is not particularly limited as long as it is a solvent-soluble acid catalyst. For example, strong inorganic acid such as sulfuric acid, nitric acid, hydrochloric acid, phosphoric acid; strong organic acid such as paratoluenesulfonic acid. Examples thereof include Lewis acids such as boron trifluoride and aluminum chloride.
Use of an organic strong acid such as p-toluenesulfonic acid is preferable in terms of catalytic activity, handleability and the like.

【0015】また、溶媒としては、使用する酸触媒との
関係で酸性溶媒が望ましく、特に酢酸、プロピオン酸、
ラク酸等の有機カルボン酸を挙げることができ、酢酸の
使用が取り扱いの便宜さなどの点で好ましい。
The solvent is preferably an acidic solvent in relation to the acid catalyst used, and particularly acetic acid, propionic acid,
Examples thereof include organic carboxylic acids such as lactic acid, and the use of acetic acid is preferable from the viewpoint of convenience of handling.

【0016】本発明の方法において、メソフェーズピッ
チに対する各種成分の添加割合は、反応及び反応条件が
適切に維持されるなら特に制限されないが、一般に、架
橋剤の量はピッチ繊維1g当たり0.0001〜0.0
5モル、酸触媒の量はピッチ繊維1g当たり0.000
1〜0.05モルであることが好ましく、溶媒の量は特
に制限はない。なお、架橋剤としてホルマリンを使用す
る場合のモル数はホルムアルデヒド換算のモル数であ
る。
In the method of the present invention, the addition ratio of various components to mesophase pitch is not particularly limited as long as the reaction and reaction conditions are appropriately maintained, but generally, the amount of the crosslinking agent is 0.0001 to 1 g of pitch fiber. 0.0
5 mol, the amount of acid catalyst is 0.000 per 1 g of pitch fiber
It is preferably 1 to 0.05 mol, and the amount of the solvent is not particularly limited. The number of moles when formalin is used as the crosslinking agent is the number of moles in terms of formaldehyde.

【0017】架橋剤の量が0.0001モル未満では酸
素原子の含有率が低下し、充分に酸化重合が行われず意
図する不融化繊維が得られない。また、架橋剤の量が
0.05モルを越えると酸素の含有率が極端に高くなる
と共に、過度の酸化によってピッチ分子の配向性が低下
するようになり、高物性の炭素繊維が得られにくい。
When the amount of the cross-linking agent is less than 0.0001 mol, the content of oxygen atoms is lowered, and the oxidative polymerization is not sufficiently carried out, so that the intended infusible fiber cannot be obtained. Further, when the amount of the cross-linking agent exceeds 0.05 mol, the oxygen content becomes extremely high and the orientation of pitch molecules is deteriorated due to excessive oxidation, which makes it difficult to obtain carbon fibers having high physical properties. ..

【0018】本発明の不融化のための酸化・重合反応の
条件は、メソフェーズピッチ繊維の表層が重点的に反応
することができるなら特に制限されないが、一般に90
〜150℃で、好ましくは110〜130℃で、0.1
〜10時間、好ましくは1〜2時間である。
The conditions of the oxidation / polymerization reaction for infusibilization of the present invention are not particularly limited as long as the surface layer of the mesophase pitch fiber can react predominantly, but generally 90
~ 150 ° C, preferably 110-130 ° C, 0.1
It is 10 hours, preferably 1 to 2 hours.

【0019】この反応温度が、90℃未満では充分に酸
化・重合を行うことができないし、また150℃を越え
ると繊維内部にまで酸化が進行するようになり、繊維内
部までも配向が乱され、充分に高い物性の炭素繊維が得
られない。
If the reaction temperature is lower than 90 ° C., sufficient oxidation / polymerization cannot be carried out. If the reaction temperature exceeds 150 ° C., the oxidation proceeds to the inside of the fiber and the orientation is disturbed to the inside of the fiber. , Carbon fibers having sufficiently high physical properties cannot be obtained.

【0020】また、反応時間は反応温度によって0.1
〜10時間の範囲で選択されるが、0.1時間未満では
反応が充分に行われず、また10時間を越えての反応時
間は実用上意味がない。
The reaction time is 0.1 depending on the reaction temperature.
The reaction time is selected within the range of 10 hours, but if the reaction time is less than 0.1 hours, the reaction will not be carried out sufficiently, and a reaction time of more than 10 hours is meaningless in practice.

【0021】本発明の酸化・重合に用いる装置は、特に
形状を問わないが、メソフェーズピッチ繊維の紡糸に続
いて連続に又は別個に行うことが出来て、通常のバッチ
式、流通式などを用いることができる。
The apparatus used for the oxidation / polymerization of the present invention is not particularly limited in shape, but it can be continuously or separately performed after spinning the mesophase pitch fiber, and a usual batch type, flow type or the like is used. be able to.

【0022】本発明の方法で得られた不融化繊維を、そ
の後常法に従って、炭化して高物性の炭素繊維又は黒鉛
繊維を製造する。
The infusible fiber obtained by the method of the present invention is then carbonized according to a conventional method to produce carbon fiber or graphite fiber having high physical properties.

【0023】炭化工程は炭素繊維の用途に応じて、反応
条件を種々選択できるが、一般に窒素、アルゴンなどの
不活性ガス下で、5〜100℃/分の昇温速度で400
〜3000℃、好ましくは900〜2500℃まで熱処
理する。
In the carbonization step, various reaction conditions can be selected according to the use of the carbon fiber, but generally, it is 400 at a temperature rising rate of 5 to 100 ° C./min under an inert gas such as nitrogen or argon.
Heat treatment is performed up to 3000C, preferably 900-2500C.

【0024】[0024]

【作用】従来法の気相酸化によるピッチ繊維の不融化処
理では、繊維内部にまで酸素が侵入し、酸化によってピ
ッチ分子の配向性が低下するために、後段の炭化過程に
おける結晶成長が阻害されるなどの理由により充分に結
晶構造を成長させることが難しく、また、導入された酸
素原子の脱離に伴って構造欠陥が生じて、高物性の炭素
繊維を得ることが難しいものであった。
[Function] In the infusibilizing treatment of the pitch fiber by the vapor phase oxidation of the conventional method, oxygen penetrates into the inside of the fiber and the orientation of the pitch molecule is lowered by the oxidation, so that the crystal growth in the subsequent carbonization process is hindered. Therefore, it is difficult to grow a crystal structure sufficiently, and structural defects occur due to desorption of introduced oxygen atoms, and it is difficult to obtain carbon fibers having high physical properties.

【0025】この場合、不融化反応温度は200〜40
0℃と高いので、この反応温度を下げて反応を抑制しよ
うとすると、反応が不均質になったり不十分になったり
する恐れがある。
In this case, the infusible reaction temperature is 200 to 40.
Since it is as high as 0 ° C., if the reaction temperature is lowered to suppress the reaction, the reaction may become inhomogeneous or insufficient.

【0026】これに対して、本発明の方法では、90〜
150℃と言う低温の反応条件下で液相で、特に酸性溶
媒中で不融化するので、その反応が迅速であり、かつ繊
維の内層にまで進行せずに表層が重点的に酸化・重合さ
れる。従って、不融化による分子配向の乱れが抑制され
て、ピッチ繊維形成時の配向を保持したまま、不融化繊
維を形成することができる。その結果、高物性、特に引
張強度の向上したメソフェーズピッチ系炭素繊維が得ら
れる。
On the other hand, according to the method of the present invention,
Since it is infusibilized in a liquid phase under a low temperature reaction condition of 150 ° C., particularly in an acidic solvent, the reaction is rapid and the surface layer is mainly oxidized and polymerized without proceeding to the inner layer of the fiber. It Therefore, the disorder of the molecular orientation due to the infusibilization is suppressed, and the infusibilized fiber can be formed while maintaining the orientation when the pitch fiber is formed. As a result, a mesophase pitch carbon fiber having high physical properties, particularly improved tensile strength can be obtained.

【0027】[0027]

【実施例】本発明は以下の実施例及び比較例により具体
的に説明されるが、これらは本発明の範囲を制限しな
い。
The present invention is illustrated by the following examples and comparative examples, which do not limit the scope of the present invention.

【0028】[0028]

【実施例1】フローテスターで測定した軟化点が245
℃のメソフェーズピッチ(メソフェーズ含有率90%)
を原料にして、溶融紡糸法により紡糸口金温度320℃
で、巻取速度170m/分で紡糸して、繊維径13μm
のメソフェーズピッチ繊維を得た。次に、プロピオン酸
溶媒にパラトルエンスルホン酸触媒0.075モル、ホ
ルマリン架橋剤0.075モル(ホルムアルデヒド換
算)を添加して反応溶液を調製した。
Example 1 The softening point measured by a flow tester is 245.
Mesophase pitch at 90 ℃ (Mesophase content 90%)
Spindle spinneret temperature of 320 ℃ by melt spinning method
At a winding speed of 170 m / min, the fiber diameter is 13 μm.
The mesophase pitch fiber of was obtained. Next, a reaction solution was prepared by adding 0.075 mol of a paratoluenesulfonic acid catalyst and 0.075 mol of a formalin crosslinking agent (in terms of formaldehyde) to a propionic acid solvent.

【0029】該反応溶液に該メソフェースピッチ繊維3
gを浸漬し、120℃で7時間反応させた後に繊維を取
り出し、130℃で真空乾燥して不融化糸を得た。この
時の不融化収率は96重量%であった。
The mesophase pitch fiber 3 is added to the reaction solution.
g was soaked and reacted at 120 ° C. for 7 hours, then the fiber was taken out and vacuum dried at 130 ° C. to obtain an infusible yarn. The infusibilization yield at this time was 96% by weight.

【0030】該不融化糸を2500℃で黒鉛化し、収率
81重量%、繊維径9.5μmの黒鉛化繊維を得た。こ
の黒鉛化繊維の引張強度は343kgf/mm2 、弾性
率54tf/mm2であった。
The infusibilized yarn was graphitized at 2500 ° C. to obtain a graphitized fiber having a yield of 81% by weight and a fiber diameter of 9.5 μm. The tensile strength of this graphitized fiber was 343 kgf / mm 2 , and the elastic modulus was 54 tf / mm 2 .

【0031】[0031]

【実施例2】プロピオン酸溶媒にパラトルエンスルホン
酸触媒0.15モル、ホルマリン架橋剤0.15モル
(ホルムアルデヒド換算)を添加して反応溶液を調製し
た。
Example 2 A reaction solution was prepared by adding 0.15 mol of a paratoluenesulfonic acid catalyst and 0.15 mol of a formalin crosslinking agent (formaldehyde conversion) to a propionic acid solvent.

【0032】該反応溶液に実施例1で得られたメソフェ
ーズピッチ繊維3gを浸漬し、120℃で5時間反応さ
せた後に繊維を取り出し、130℃で真空乾燥して不融
化糸を得た。この時の不融化収率は100重量%であっ
た。
3 g of the mesophase pitch fiber obtained in Example 1 was dipped in the reaction solution, reacted at 120 ° C. for 5 hours, taken out of the fiber, and vacuum dried at 130 ° C. to obtain an infusibilized yarn. The infusibilization yield at this time was 100% by weight.

【0033】該不融化糸を2500℃で黒鉛化し、収率
81重量%、繊維径9.5μmの黒鉛化繊維を得た。こ
の黒鉛化繊維の引張強度は370kgf/mm2 、弾性
率64tf/mm2であった。
The infusible yarn was graphitized at 2500 ° C. to obtain graphitized fiber having a yield of 81% by weight and a fiber diameter of 9.5 μm. The tensile strength of this graphitized fiber was 370 kgf / mm 2 , and the elastic modulus was 64 tf / mm 2 .

【0034】[0034]

【比較例1】実施例1で用いたメソフェースピッチ繊維
を、空気中で1.8℃/分の昇温温度で300℃まで加
熱し、収率106.7重量%の不融化糸を得た。
Comparative Example 1 The mesophase pitch fiber used in Example 1 was heated to 300 ° C. in air at a temperature rising temperature of 1.8 ° C./min to obtain an infusible yarn having a yield of 106.7% by weight. It was

【0035】該不融化糸を2500℃で黒鉛化し、収率
88重量%、繊維径9.9μmの黒鉛化繊維を得た。こ
の黒鉛化繊維の引張強度は307kgf/mm2 、弾性
率56tf/mm2であった。これらの結果を下記表1
にまとめて示す。
The infusible yarn was graphitized at 2500 ° C. to obtain a graphitized fiber having a yield of 88% by weight and a fiber diameter of 9.9 μm. The tensile strength of this graphitized fiber was 307 kgf / mm 2 , and the elastic modulus was 56 tf / mm 2 . These results are shown in Table 1 below.
Are summarized in.

【0036】[0036]

【表1】 [Table 1]

【0037】[0037]

【発明の効果】本発明の方法により、メソフェーズピッ
チ繊維を低温で液相酸化・重合することにより、不融化
による分子配向の乱れが抑制されて、ピッチ繊維形成時
の配向を保持したまま、不融化繊維を形成することがで
きる。従って高物性のメソフェーズピッチ系炭素繊維が
得られる効果がある。
EFFECTS OF THE INVENTION By the method of the present invention, the mesophase pitch fibers are liquid-phase oxidized and polymerized at a low temperature, whereby the disorder of the molecular orientation due to infusibilization is suppressed, and the misalignment of the mesophase pitch fibers is prevented while maintaining the orientation during pitch fiber formation. Fused fibers can be formed. Therefore, there is an effect that a mesophase pitch carbon fiber having high physical properties can be obtained.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 メソフェーズピッチを常法に従って溶融
紡糸してピッチ繊維とした後、該ピッチ繊維を酸触媒と
架橋剤の存在下で溶媒中で液相酸化・重合することによ
り不融化することを特徴とする、メソフェーズピッチ系
炭素繊維の製造方法。
1. Mesophase pitch is melt-spun according to a conventional method to give pitch fibers, and the pitch fibers are infusibilized by liquid-phase oxidation / polymerization in a solvent in the presence of an acid catalyst and a crosslinking agent. A method for producing a mesophase pitch carbon fiber, which is characterized.
【請求項2】 溶媒としてカルボン酸などの酸性溶媒を
使用する、請求項1記載のメソフェーズピッチ系炭素繊
維の製造方法。
2. The method for producing mesophase pitch carbon fiber according to claim 1, wherein an acidic solvent such as carboxylic acid is used as the solvent.
【請求項3】 酸化・重合条件が90〜150℃で0.
1〜10時間であり、かつピッチ繊維に対する架橋剤及
び酸触媒の混合比が、夫々ピッチ繊維1g当たり0.0
001〜0.05モル及び0.0001〜0.05モル
である、請求項1記載のメソフェーズピッチ系炭素繊維
の製造方法。
3. Oxidation / polymerization conditions of 90 to 150 ° C.
1 to 10 hours, and the mixing ratio of the cross-linking agent and the acid catalyst to the pitch fiber is 0.0 per 1 g of the pitch fiber, respectively.
The method for producing a mesophase pitch carbon fiber according to claim 1, wherein the amount is 001 to 0.05 mol and 0.0001 to 0.05 mol.
JP20176892A 1991-07-18 1992-07-07 Production of mesophase pitch-based carbon fiber Pending JPH05214613A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20176892A JPH05214613A (en) 1991-07-18 1992-07-07 Production of mesophase pitch-based carbon fiber

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP3-202131 1991-07-18
JP20213191 1991-07-18
JP20176892A JPH05214613A (en) 1991-07-18 1992-07-07 Production of mesophase pitch-based carbon fiber

Publications (1)

Publication Number Publication Date
JPH05214613A true JPH05214613A (en) 1993-08-24

Family

ID=26512977

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20176892A Pending JPH05214613A (en) 1991-07-18 1992-07-07 Production of mesophase pitch-based carbon fiber

Country Status (1)

Country Link
JP (1) JPH05214613A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110230124A (en) * 2019-05-21 2019-09-13 湖南东映碳材料科技有限公司 A kind of method that Mesophase Pitch Fiberss oil

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110230124A (en) * 2019-05-21 2019-09-13 湖南东映碳材料科技有限公司 A kind of method that Mesophase Pitch Fiberss oil

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