JPH11124742A - Production of carbon fiber - Google Patents

Production of carbon fiber

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Publication number
JPH11124742A
JPH11124742A JP29295197A JP29295197A JPH11124742A JP H11124742 A JPH11124742 A JP H11124742A JP 29295197 A JP29295197 A JP 29295197A JP 29295197 A JP29295197 A JP 29295197A JP H11124742 A JPH11124742 A JP H11124742A
Authority
JP
Japan
Prior art keywords
carbon fiber
pitch
modified pitch
solution
spinning
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
JP29295197A
Other languages
Japanese (ja)
Other versions
JP3994488B2 (en
Inventor
Takashi Yoshimura
貴史 吉村
Yukio Sakai
幸男 酒井
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 Gas Chemical Co Inc
Original Assignee
Mitsubishi Gas Chemical Co Inc
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 Gas Chemical Co Inc filed Critical Mitsubishi Gas Chemical Co Inc
Priority to JP29295197A priority Critical patent/JP3994488B2/en
Publication of JPH11124742A publication Critical patent/JPH11124742A/en
Application granted granted Critical
Publication of JP3994488B2 publication Critical patent/JP3994488B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To obtain carbon fiber that has excellent strength and modulus and is useful as a reinforcing material for a variety of composite materials by dissolving a prescribed amount of modified pitch in a solution of acrylic polymer in a solvent, spinning the solution to fiber, and firing the fiber. SOLUTION: To a solution of an acrylic polymer as polyacrylonitrile in a solvent, is added a modified pitch that is readily soluble in at least one polar organic solvents selected from dimethyl sulfoxide, dimethylformamide and dimethyl-acetamide in a concentration of 0.1-30 wt.%. Then, mixture is spun into filaments and fired to give the objective carbon fiber. In a preferred embodiment, the modified pitch has an anisotropic texture and is carbonized without deformation, when it is heated in an inert atmosphere.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は強度と弾性率ともに優れ
た高性能炭素繊維製造法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a high-performance carbon fiber having excellent strength and elastic modulus.

【0002】[0002]

【従来の技術】従来から炭素繊維はその優れた比強度・
比弾性率から、宇宙航空・スポーツ、レジャー産業等の
幅広い分野において、各種複合材の強化材として工業的
に利用されている。現在、工業的規模で生産されている
炭素繊維は、ポリアクリロニトリル主成分の合成繊維を
原料とするPAN系炭素繊維と、石油・石炭・合成ピッ
チ等を原料とするピッチ系炭素繊維に大きく2種類分け
られる。
2. Description of the Related Art Conventionally, carbon fibers have a high specific strength.
Due to its specific elastic modulus, it is industrially used as a reinforcing material for various composite materials in a wide range of fields such as the aerospace / sports and leisure industries. Currently, there are two major types of carbon fibers produced on an industrial scale: PAN-based carbon fibers made from synthetic fibers mainly composed of polyacrylonitrile and pitch-based carbon fibers made from petroleum, coal, synthetic pitch and the like. Divided.

【0003】PAN系炭素繊維は主に高強度・高伸度に
優れるが、原料に由来し難黒鉛化性であることから、弾
性率が低いという欠点がある。弾性率向上を図るには2
000℃を越す高温での焼成が有効であるが、同時に強
度の低下を招く。また高温焼成による炉の低寿命化な
ど、コストアップにつながる要因が増え、工業的規模で
は不利になる。
[0003] PAN-based carbon fibers are mainly excellent in high strength and high elongation, but have a drawback that they have a low elastic modulus because they are derived from raw materials and are hardly graphitizable. 2 to improve elastic modulus
Baking at a high temperature exceeding 000 ° C. is effective, but at the same time causes a decrease in strength. Factors that lead to cost increases, such as shortening of furnace life due to high-temperature firing, are disadvantageous on an industrial scale.

【0004】ピッチ系炭素繊維に関しては大きく分けて
等方性ピッチ由来のものと、異方性ピッチ由来のものが
あるが、高性能を発現するには一般的には異方性ピッチ
が用いられる。異方性ピッチ原料からの炭素繊維は、そ
の原料の易黒鉛化の性質から高弾性・高強度に優れるが
伸度が低く、工業的には炭素繊維の生産性や複合化の際
のハンドリング性に劣るという欠点がある。
[0004] Pitch-based carbon fibers can be roughly divided into those derived from isotropic pitch and those derived from anisotropic pitch. Anisotropic pitch is generally used to exhibit high performance. . Carbon fiber from anisotropic pitch raw material has high elasticity and high strength due to the property of easy graphitization of raw material, but has low elongation, and industrially, carbon fiber productivity and handling property at the time of compounding There is a disadvantage that it is inferior.

【0005】これらのことからPAN系炭素繊維とピッ
チ系炭素繊維の両者の欠点を補うため、両者の複合化の
検討が種々なされている。例えばアクリル系重合体にピ
ッチを混合し紡糸・焼成する炭素繊維製造法(特開平2
−47311号)が提案されている。しかし、この方法
は基本的には単なる混合であるため、混合ピッチを非常
に微細に粉砕しておく必要があるなど、工業的規模での
利用には不利である。さらに混合するピッチが軟化点を
有するため、炭素繊維製造工程中の耐炎化時にピッチの
不融化を同時に最適に行わなければピッチが軟化溶融す
る恐れがあるなどの工程の複雑化につながり、炭素繊維
製造のコストアップの原因となりかねない。
[0005] In view of the above, in order to compensate for the disadvantages of both the PAN-based carbon fiber and the pitch-based carbon fiber, various studies have been made on the compounding of both. For example, a carbon fiber production method in which pitch is mixed with an acrylic polymer, and then spun and fired (Japanese Patent Laid-Open No.
-47311) has been proposed. However, since this method is basically just mixing, it is disadvantageous for use on an industrial scale, for example, it is necessary to pulverize the mixing pitch very finely. Furthermore, since the pitch to be mixed has a softening point, if the infusibilization of the pitch is not performed simultaneously and optimally at the time of flame resistance during the carbon fiber production process, the pitch may be softened and melted, leading to a complicated process, and the carbon fiber It may cause an increase in manufacturing cost.

【0006】[0006]

【発明が解決しようとする課題】本発明の目的は、上記
の如き高性能炭素繊維製造の現状に鑑み、強度、弾性率
ともに優れた炭素繊維の工業的に有利な製造法を提供す
ることにある。
SUMMARY OF THE INVENTION An object of the present invention is to provide an industrially advantageous method for producing carbon fiber having excellent strength and elastic modulus in view of the above-mentioned current situation of producing high-performance carbon fiber. is there.

【0007】[0007]

【課題を解決するための手段】本発明者らは上記の如き
課題を有する炭素繊維製造法について鋭意検討した結
果、ポリアクリロニトリル系炭素繊維を製造するに際し
て、アクリル系重合体溶媒溶液に、変性されたピッチを
0.1〜30重量%溶解混合し、それを紡糸・焼成する
ことによって、従来の製造工程をほとんど変更すること
なく、強度を保持しつつ、弾性率を向上させることがで
きることを見出し、本発明に到達した。すなわち本発明
は、アクリル系重合体溶媒溶液に、変性されたピッチを
0.1〜30重量%溶解混合し、紡糸・焼成することを
特徴とする炭素繊維の製造法である。
Means for Solving the Problems The inventors of the present invention have conducted intensive studies on a method for producing carbon fibers having the above-mentioned problems, and as a result, when producing polyacrylonitrile-based carbon fibers, they have been modified into an acrylic polymer solvent solution. It has been found that by mixing and dissolving 0.1 to 30% by weight of the prepared pitch and spinning and baking it, the elastic modulus can be improved while maintaining the strength without substantially changing the conventional manufacturing process. Reached the present invention. That is, the present invention is a method for producing carbon fibers, which comprises dissolving and mixing 0.1 to 30% by weight of a modified pitch in an acrylic polymer solvent solution and spinning and firing.

【0008】[0008]

【発明の実施の形態】本発明において用いられるアクリ
ロニトリル系重合体は特に限定されるものではないが、
炭素繊維の機械的物性を考慮すると、少なくとも90モ
ル%以上のアクリロニトリルと、10モル%以下のアク
リロニトリルと共重合可能なビニル系モノマー、例えば
アクリル酸、メタクリル酸、イタコン酸等の不飽和カル
ボン酸及びその塩類、アクリル酸メチル、アクリル酸ブ
チル、アクリルアミドや、アリルスルホン酸及びそれの
塩類などをからなるアクリロニトリル系重合体が挙げら
れる。
BEST MODE FOR CARRYING OUT THE INVENTION The acrylonitrile polymer used in the present invention is not particularly limited.
Considering the mechanical properties of carbon fibers, at least 90 mol% or more of acrylonitrile and 10 mol% or less of vinyl monomers copolymerizable with acrylonitrile, for example, unsaturated carboxylic acids such as acrylic acid, methacrylic acid, and itaconic acid; Examples thereof include acrylonitrile-based polymers comprising salts thereof, methyl acrylate, butyl acrylate, acrylamide, allylsulfonic acid and salts thereof.

【0009】アクリロニトリルとビニル系モノマーの重
合方法は特に限定されるものではなく、従来公知の方法
である、溶液、懸濁、乳化重合を適用することができ
る。これらのアクリロニトリル系重合体は紡糸するため
に、一般的なポリアクリロニトリル系重合物の紡糸原液
に使用される溶媒である、ジメチルスルホキシド(DM
SO)、ジメチルホルムアミドおよびジメチルアセトア
ミド等の極性有機溶媒の溶液にして用いられる。
The method of polymerizing acrylonitrile and vinyl monomer is not particularly limited, and a conventionally known method such as solution, suspension and emulsion polymerization can be applied. These acrylonitrile-based polymers are dimethylsulfoxide (DM), which is a solvent used for spinning of a general polyacrylonitrile-based polymer for spinning.
SO), dimethylformamide and dimethylacetamide.

【0010】本発明で用いられる変性ピッチの原料は、
石炭、石油、合成系のいずれのピッチも用いることがで
きる。このようなピッチは偏光顕微鏡下の光学組織で、
等方性、異方性は問わないが、本発明の目的である高性
能炭素繊維の製造には異方性が好ましく用いられる。
The raw material of the modified pitch used in the present invention is:
Any pitch of coal, petroleum and synthetic system can be used. Such a pitch is an optical structure under a polarizing microscope,
Although the isotropic property and the anisotropy are not limited, the anisotropic property is preferably used in the production of the high performance carbon fiber which is the object of the present invention.

【0011】本発明で用いられるピッチ、特に異方性ピ
ッチでは原料ピッチのDMSO等の極性有機溶媒に対す
る溶解性が低く、かつ軟化点を有するため、極性溶媒に
対して溶解を有し、かつ軟化点・融点等を持たず、窒素
等不活性雰囲気中でも加熱により変形することなく炭素
化できるように変性する必要がある。変性は例えば硫酸
や酢酸等の酸水溶液中に細かく粉砕された原料ピッチを
分散し、50℃付近の温度条件で過酸化水素などの酸化
剤を添加し反応させることで達成され、該反応後、濾過
・水洗・乾燥により変性されたピッチが得られる。十分
に変性されたピッチはDMSO等の極性有機溶媒に容易
に溶解する。また、熱に対し不融でさらなる加熱にも形
態を維持しながら炭素化していき、原料ピッチが光学的
異方性である場合は処理ピッチも異方性組織を保持して
いる。
The pitch used in the present invention, particularly the anisotropic pitch, has low solubility in a polar organic solvent such as DMSO and has a softening point, so that the pitch has a solubility in a polar solvent and a softening point. It is necessary to modify the material so as not to have a point and a melting point and to be carbonized without being deformed by heating even in an inert atmosphere such as nitrogen. Modification is achieved, for example, by dispersing the finely ground raw material pitch in an aqueous acid solution such as sulfuric acid or acetic acid, and reacting by adding an oxidizing agent such as hydrogen peroxide at a temperature condition of about 50 ° C., after the reaction, A modified pitch is obtained by filtration, washing and drying. Well-modified pitch readily dissolves in polar organic solvents such as DMSO. Further, it is infused with heat and is carbonized while maintaining its form even when further heated. When the raw material pitch is optically anisotropic, the treated pitch also retains an anisotropic structure.

【0012】アクリル系重合物と変性されたピッチとの
混合には、特別な操作は必要ない。溶液重合より紡糸原
液が得られる場合、従来の手順でアクリロニトリルと共
重合成分の重合を行い、これに変性されたピッチを添加
し、室温で溶解混合する。懸濁、乳化重合のように得ら
れた重合物をあらためて有機溶媒に溶解し紡糸原液とす
る場合は、その有機溶媒に変性されたピッチを溶解して
からポリマーを溶解しても良いし、その逆でもよい。
No special operation is required for mixing the acrylic polymer with the modified pitch. When a spinning stock solution is obtained from solution polymerization, acrylonitrile and a copolymer component are polymerized by a conventional procedure, a modified pitch is added thereto, and the mixture is dissolved and mixed at room temperature. Suspension, when the obtained polymer is re-dissolved in an organic solvent to obtain a spinning dope as in emulsion polymerization, the polymer may be dissolved after dissolving the modified pitch in the organic solvent, The reverse is also acceptable.

【0013】アクリル系重合物と変性されたピッチとの
混合割合は、0.1〜30重量%、好ましくは2〜15
重量%である。0.1重量%未満ではその添加効果が明
確でなくなり、30重量%以上では紡糸工程での延伸が
困難になり、糸切れなども発生する。
The mixing ratio between the acrylic polymer and the modified pitch is 0.1 to 30% by weight, preferably 2 to 15% by weight.
% By weight. If the amount is less than 0.1% by weight, the effect of the addition becomes unclear, and if the amount is more than 30% by weight, stretching in the spinning step becomes difficult, and yarn breakage or the like occurs.

【0014】本発明における紡糸方法は、アクリル系炭
素繊維の製造に利用される従来公知の方法を適用するこ
とができ、その後の延伸や乾燥緻密化により炭素繊維プ
レカーサーを得ることができる。得られたプレカーサー
の耐炎化、焼成は、溶解したピッチが熱に対して変形せ
ず炭素化することから、従来の条件をそのまま適用する
ことができる。
As the spinning method in the present invention, a conventionally known method used in the production of acrylic carbon fibers can be applied, and a carbon fiber precursor can be obtained by subsequent drawing or dry densification. The flame retardation and calcination of the obtained precursor can be carried out under the conventional conditions, since the dissolved pitch is carbonized without being deformed by heat.

【0015】[0015]

【実施例】次に実施例により本発明を具体的に説明す
る。ただし本発明はこれらの実施例により制限されるも
のではない。
Next, the present invention will be described in detail with reference to examples. However, the present invention is not limited by these examples.

【0016】実施例1 アクリロニトリル95モル%、メチルアクリレート4.
5モル%、イタコン酸0.5モル%のモノマー組成物
を、重合後の重合物濃度が20%付近になるようにジメ
チルスルホキシド中に仕込み、アゾビスイスブチルニト
リル(AIBN)を開始剤、ドデシルメルカプタンを連
鎖移動剤に用い65℃で溶液重合を行い、アクリル系重
合体を得た。一方、変性ピッチ調製用の原料ピッチには
ナフタレンからHF/BF3 触媒を用いて重合して得ら
れたメソフェーズ100%の合成ピッチを用いた。この
原料ピッチをコーヒーミルで粉砕し、50℃に加熱され
た硫酸水溶液中に攪拌下分散した。これに過酸化水素を
少しずつ添加し反応を開始した。ビッチに対して5倍量
の過酸化水素の全量を添加した後、一晩の反応を行い、
反応終了後ガラスフィルターにより濾過し、イオン交換
水で濾液が酸性を示さなくなるまで水洗を行った後、減
圧乾燥して変性ピッチを得た。得られた変性ピッチは室
温でジメチルスルホキシドやジメチルホルムアミドに容
易に溶解することを確認できた。また粉末状態の変性ピ
ッチを窒素雰囲気下、環状炉を用い1000℃まで焼成
を行ったが、焼成後の粒子の融着や変形が見られず炭素
化することが確認できた。この焼成粉を樹脂埋めし研磨
した後、光学組織観察を行ったが、原料と同様メソフェ
ーズ100%であることが観察された。このようにして
調製した変性ピッチを、重合物に対し10%添加し撹拌
下溶解混合行った。溶解確認後、減圧脱泡を行いこれを
紡糸原液とした。この紡糸原液をDMSO65%よりな
る水系凝固浴中に、0.08mmφ・100Hの紡糸口
金を通し吐出した後、熱水中で3倍に延伸し、続いて1
35℃のグリセリン浴中で2倍に延伸した。その後十分
水洗し、緊張下150℃の乾燥・180℃の熱処理を行
い炭素繊維プレカーサーとした。この炭素繊維プレカー
サーを緊張下220℃で30分そして250℃で30分
の熱処理を空気中で行い耐炎化糸とした。この耐炎化糸
を緊張下、高純度窒素中毎分10℃で1000℃まで昇
温し炭素繊維を得た。得られた炭素繊維の性能は、引張
強度189kg/mm2 、弾性率18t/mm2 であっ
た。
Example 1 95 mol% of acrylonitrile, methyl acrylate
A monomer composition of 5 mol% and 0.5 mol% of itaconic acid was charged into dimethyl sulfoxide so that the concentration of the polymer after polymerization was about 20%, and azobiswisthbutylnitrile (AIBN) was used as an initiator and dodecyl. Solution polymerization was carried out at 65 ° C. using mercaptan as a chain transfer agent to obtain an acrylic polymer. On the other hand, a synthetic pitch of 100% mesophase obtained by polymerizing naphthalene using HF / BF 3 catalyst was used as a raw material pitch for preparing a modified pitch. This raw material pitch was pulverized by a coffee mill and dispersed in a sulfuric acid aqueous solution heated to 50 ° C. with stirring. Hydrogen peroxide was added little by little to start the reaction. After adding 5 times the total amount of hydrogen peroxide to the bitch, perform the reaction overnight,
After completion of the reaction, the mixture was filtered through a glass filter, washed with ion-exchanged water until the filtrate no longer showed acidity, and dried under reduced pressure to obtain a modified pitch. It was confirmed that the obtained modified pitch easily dissolved in dimethylsulfoxide and dimethylformamide at room temperature. The modified pitch in a powder state was fired in a nitrogen atmosphere in an annular furnace up to 1000 ° C., but no fusion or deformation of the fired particles was observed and carbonization was confirmed. After the baked powder was filled with a resin and polished, optical structure observation was performed, and it was observed that the mesophase was 100% similarly to the raw material. 10% of the modified pitch thus prepared was added to the polymer and dissolved and mixed with stirring. After confirming dissolution, defoaming was performed under reduced pressure to obtain a spinning stock solution. The undiluted spinning solution is discharged through a spinneret of 0.08 mmφ · 100H into an aqueous coagulation bath composed of 65% DMSO, and then stretched three times in hot water.
The film was stretched twice in a glycerin bath at 35 ° C. Thereafter, it was sufficiently washed with water and dried under a tension at 150 ° C. and a heat treatment at 180 ° C. to obtain a carbon fiber precursor. The carbon fiber precursor was subjected to a heat treatment under tension at 220 ° C. for 30 minutes and at 250 ° C. for 30 minutes in air to obtain an oxidized yarn. The flame-resistant yarn was heated to 1000 ° C. at 10 ° C./min in high-purity nitrogen under tension to obtain carbon fibers. The performance of the obtained carbon fiber was a tensile strength of 189 kg / mm 2 and an elastic modulus of 18 t / mm 2 .

【0017】比較例1 実施例1において、変性ピッチを混合しないでポリアク
リロニトリル系のみよりなる炭素繊維を同様に製造し
た。得られた炭素繊維の性能は、引張強度180kg/
mm2 、弾性率14t/mm2 であった。
Comparative Example 1 In Example 1, a carbon fiber consisting only of polyacrylonitrile was produced in the same manner without mixing modified pitch. The performance of the obtained carbon fiber was a tensile strength of 180 kg /
mm 2 , and the elastic modulus was 14 t / mm 2 .

【0018】実施例2 実施例1と同組成のモノマーより、懸濁重合にてポリア
クリロニトリル系共重合体を合成した。DMSO溶媒に
後で溶解する懸濁重合物に対し、10%の変性されたピ
ッチを添加溶解した。この変性ピッチのDMSO溶液を
50℃に保温し、これに重合物濃度が20%付近になる
ように重合物を少しずつ溶解し、全量溶解後減圧脱泡を
行い紡糸原液を調製した。この紡糸原液を実施例1と同
様に紡糸し、炭素繊維の調製を行った。得られた炭素繊
維の性能は、引張強度205kg/mm2 、弾性率20
t/mm2 であった。
Example 2 A polyacrylonitrile copolymer was synthesized from monomers having the same composition as in Example 1 by suspension polymerization. 10% of the modified pitch was added and dissolved in the suspension polymer which was later dissolved in the DMSO solvent. The DMSO solution of the modified pitch was kept at 50 ° C., and the polymer was dissolved little by little so that the polymer concentration became about 20%. After dissolving the whole amount, defoaming was performed under reduced pressure to prepare a spinning stock solution. This spinning stock solution was spun in the same manner as in Example 1 to prepare a carbon fiber. The properties of the obtained carbon fiber were as follows: a tensile strength of 205 kg / mm 2 and an elastic modulus of 20 kg / mm 2 .
t / mm 2 .

【0019】比較例2 実施例2において、変性ピッチを混合しないでポリアク
リロニトリル系のみよりなる炭素繊維を同様に製造し
た。得られた炭素繊維の性能は、引張強度191kg/
mm2 、弾性率16t/mm2 であった。
Comparative Example 2 In Example 2, a carbon fiber consisting of only polyacrylonitrile was produced in the same manner without mixing modified pitch. The performance of the obtained carbon fiber was 191 kg / tensile strength.
mm 2 and an elastic modulus of 16 t / mm 2 .

【0020】[0020]

【発明の効果】以上の実施例からも明らかなように、本
発明の炭素繊維の製造方法では、従来のポリアクリロニ
トリル系炭素繊維用の重合物の重合方法、及び炭素繊維
調製方法を何ら変更することなく採用することができ、
ポリアクリロニトリル系炭素繊維の強度を下げることな
く弾性率を向上させることができる。従って本発明によ
り強度と弾性率ともに優れた高性能炭素繊維を工業的に
有利に製造することができ、本発明の工業的意義は大き
い。
As is clear from the above examples, in the method for producing carbon fiber of the present invention, the conventional method for polymerizing a polymer for polyacrylonitrile-based carbon fiber and the method for preparing carbon fiber are changed. Can be adopted without
The elastic modulus can be improved without lowering the strength of the polyacrylonitrile-based carbon fiber. Therefore, according to the present invention, a high-performance carbon fiber excellent in both strength and elastic modulus can be industrially advantageously produced, and the present invention has great industrial significance.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】アクリル系重合体溶媒溶液に、変性された
ピッチを0.1〜30重量%溶解混合し、紡糸・焼成す
ることを特徴とする炭素繊維の製造法。
1. A method for producing carbon fibers, comprising dissolving and mixing 0.1 to 30% by weight of a modified pitch in an acrylic polymer solvent solution and spinning and firing.
【請求項2】変性されたピッチが、ジメチルスルホキシ
ド、ジメチルホルムアミドおよびジメチルアセトアミド
から選ばれた一種以上の極性有機溶媒に容易に溶解する
ものである請求項1記載の炭素繊維製造法。
2. The method according to claim 1, wherein the modified pitch is easily dissolved in one or more polar organic solvents selected from dimethylsulfoxide, dimethylformamide and dimethylacetamide.
【請求項3】変性されたピッチが、異方性組織を有し、
不活性雰囲気中で加熱により変形することなく炭素化す
るものである請求項1記載の炭素繊維製造法。
3. The modified pitch has an anisotropic structure,
The carbon fiber production method according to claim 1, wherein the carbonization is performed without deformation by heating in an inert atmosphere.
JP29295197A 1997-10-24 1997-10-24 Carbon fiber manufacturing method Expired - Fee Related JP3994488B2 (en)

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JP3994488B2 JP3994488B2 (en) 2007-10-17

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100759102B1 (en) 2006-05-29 2007-09-19 주식회사 나노테크닉스 Preparation method of two-phase carbon nanofibers and activated carbon nanofibers by electrospinning from polyacrylonitrile/pitch blend solutions
JP2012507638A (en) * 2008-11-06 2012-03-29 インダストリー ファウンデーション オブ チョンナム ナショナル ユニバーシティ Carbon nanofiber having skin-core structure, method for producing the same, and product containing said carbon nanofiber
US8865106B2 (en) 2011-12-26 2014-10-21 Industrial Technology Research Institute Composite raw material, carbon fiber material and method for forming the same
CN114687011A (en) * 2022-05-06 2022-07-01 广州碳加科技有限公司 Preparation method of low-cost carbon fiber precursor

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100759102B1 (en) 2006-05-29 2007-09-19 주식회사 나노테크닉스 Preparation method of two-phase carbon nanofibers and activated carbon nanofibers by electrospinning from polyacrylonitrile/pitch blend solutions
JP2012507638A (en) * 2008-11-06 2012-03-29 インダストリー ファウンデーション オブ チョンナム ナショナル ユニバーシティ Carbon nanofiber having skin-core structure, method for producing the same, and product containing said carbon nanofiber
US8865106B2 (en) 2011-12-26 2014-10-21 Industrial Technology Research Institute Composite raw material, carbon fiber material and method for forming the same
CN114687011A (en) * 2022-05-06 2022-07-01 广州碳加科技有限公司 Preparation method of low-cost carbon fiber precursor

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