JPH0633530B2 - Carbon fiber and manufacturing method thereof - Google Patents

Carbon fiber and manufacturing method thereof

Info

Publication number
JPH0633530B2
JPH0633530B2 JP59193247A JP19324784A JPH0633530B2 JP H0633530 B2 JPH0633530 B2 JP H0633530B2 JP 59193247 A JP59193247 A JP 59193247A JP 19324784 A JP19324784 A JP 19324784A JP H0633530 B2 JPH0633530 B2 JP H0633530B2
Authority
JP
Japan
Prior art keywords
pitch
carbon fiber
temperature
less
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.)
Expired - Lifetime
Application number
JP59193247A
Other languages
Japanese (ja)
Other versions
JPS6183319A (en
Inventor
郁夫 瀬尾
泰雄 坂口
健 柏舘
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.)
Kureha Corp
Original Assignee
Kureha 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 Kureha Corp filed Critical Kureha Corp
Priority to JP59193247A priority Critical patent/JPH0633530B2/en
Priority to CA000490155A priority patent/CA1262007A/en
Priority to DE3546613A priority patent/DE3546613C2/de
Priority to FR8513616A priority patent/FR2570395B1/en
Priority to GB08522741A priority patent/GB2164351B/en
Priority to DE19853532785 priority patent/DE3532785A1/en
Publication of JPS6183319A publication Critical patent/JPS6183319A/en
Priority to US07/293,563 priority patent/US4863708A/en
Publication of JPH0633530B2 publication Critical patent/JPH0633530B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Working-Up Tar And Pitch (AREA)
  • Inorganic Fibers (AREA)

Description

【発明の詳細な説明】 本発明は、新規なピツチ系炭素繊維及びその製造方法に
関するものである。更に詳しくは、本発明は、ナフタリ
ンを原料とし、PAN系炭素繊維に匹敵する特性を有す
る新規な炭素繊維とその炭素繊維の製造方法に関するも
のである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a novel Pitch-based carbon fiber and a method for producing the same. More specifically, the present invention relates to a novel carbon fiber having naphthalene as a raw material and having characteristics comparable to those of PAN-based carbon fiber, and a method for producing the carbon fiber.

現在市販されている炭素繊維は、ポリアクリルニトリル
(PAN)を原料とするPAN系炭素繊維とピツチ類を
原料とするピツチ系炭素繊維とに原料によつて分類され
ており、一般的にPAN系炭素繊維はピツチ系炭素繊維
に比較して、特に引張強さの点において、優れた特性を
有するために、高強度、高弾性率の高性能の炭素繊維と
してはこれまでPAN系炭素繊維がその主流となつてい
た。しかしながら、PAN系炭素繊維では、原料が高価
であり且つ炭化収率も悪いので、経済性の点で優位に立
ち得るピツチを原料として、PAN系炭素繊維と同等の
引張強さ及び引張弾性率を有するピツチ系炭素繊維を製
造する方法の研究がなされ、いくつかの方法が提案され
ている。
The carbon fibers currently on the market are classified according to the raw material into PAN-based carbon fibers made of polyacrylonitrile (PAN) and Pitch-based carbon fibers made of pits as a raw material, and generally PAN-based carbon fibers. Since carbon fibers have excellent properties in particular in terms of tensile strength as compared with Pitch-based carbon fibers, PAN-based carbon fibers have hitherto been used as high-performance carbon fibers having high strength and high elastic modulus. It was the mainstream. However, since the PAN-based carbon fiber is expensive and the carbonization yield is poor, it is possible to obtain the same tensile strength and tensile elastic modulus as those of the PAN-based carbon fiber by using the pitch, which is advantageous in terms of economy, as the raw material. Research on a method for producing the Pitch-based carbon fiber has been made, and several methods have been proposed.

例えば、石油系ピツチ、コールタールピツチ及びアセナ
フチレンピツチを350〜500℃で、約40〜90重
量%のメン相が生ずるのに十分な時間加熱し、紡糸温度
で非チキントロピー性で10〜200ポイズの粘度を有
する炭素質ピツチを紡糸し、この紡糸繊維を酸素含有雰
囲気中て250〜400℃で不融化し、ついで得られた
不融解性繊維を不活性雰囲気中で少なくとも1000℃
に加熱し、ついで約2500℃以上に加熱するたことに
よつて、(112)クロス格子線及び(100)と(1
01)線の存在によつて特徴づけられるX線回折パター
ン、すなわち高度の三次元構造を有し、3.37Å以下の層
間隔、1000Å以上の見掛け積層寸法(La)及び1
000Å以上の見掛け積層高さ(Lc)を奏する黒鉛繊
維が製造されることが報告されている(特開昭49−1
9127)。
For example, petroleum-based pitches, coal tar pitches and acenaphthylene pitches are heated at 350-500 ° C. for a time sufficient to produce about 40-90% by weight of the menh phase and are non-chicken tropic at 10 to 10 at spinning temperatures. A carbonaceous pitch having a viscosity of 200 poise is spun, the spun fiber is infusibilized in an oxygen-containing atmosphere at 250 to 400 ° C., and the infusible fiber obtained is then at least 1000 ° C. in an inert atmosphere.
By heating to (1100) and then to (1100) and (100) and (1)
01) X-ray diffraction pattern characterized by the presence of lines, ie having a highly three-dimensional structure, a layer spacing of 3.37Å or less, an apparent lamination dimension (La) of 1000Å or more and 1
It has been reported that a graphite fiber having an apparent laminated height (Lc) of 000Å or more is produced (Japanese Patent Laid-Open No. 49-1).
9127).

上述の特開昭49−19127の開示のように、従来、
ピツチ系の高性能炭素繊維を製造するためには、メソフ
エーズピツチを用いることが必須であるとされていた。
これは分子配向を有するメソフエーズピツチを溶融紡糸
すると、微結晶が繊維軸に平行に配列しやすいというた
めであつた。しかしながらメソフエーズピツチは、一般
的に軟化点が高いので、溶融紡糸温度が高くなり、熱的
に不安定となる欠点がある。またメソフエーズピツチは
等方性ピツチとピツチ液晶が混在する不均一な混合物で
あるので、均一なピツチ繊維を得ることが困難であると
されていた。
As disclosed in Japanese Patent Laid-Open No. 49-19127 described above,
It has been said that the use of mesophase pitch is essential for producing a pitch-based high performance carbon fiber.
This is because when melt-spun mesophase pitches having a molecular orientation, fine crystals are easily aligned parallel to the fiber axis. However, since the mesophase pitch generally has a high softening point, it has a drawback that the melt spinning temperature becomes high and it becomes thermally unstable. Further, since the mesophase pitch is an inhomogeneous mixture in which isotropic pitch and pitch liquid crystal are mixed, it has been considered difficult to obtain uniform pitch fiber.

上述の欠点を解決するために、紡糸原料ピツチの段階で
必ずしも光学的に異方性ではないが、紡糸性に優れてお
り、紡糸あるいは焼成段階で光学的に異方性に変換する
紡糸原料ピツチ及びそれを用いた炭素繊維の製造方法が
提案されている。
In order to solve the above-mentioned drawbacks, the spinning raw material pitch is not necessarily optically anisotropic at the stage of the spinning raw material pitch, but has excellent spinnability and is converted into optically anisotropic at the spinning or firing stage. And methods for producing carbon fibers using the same have been proposed.

例えば、光学的に等方性のプリメソフエーズ炭素質又は
光学的に等方性のプリメソフエーズ炭素質を主体とする
ピツチ状物質を実質的にメソフエーズ炭素質量が増加し
ない条件で紡糸し、次いで不融化処理したのち、炭化処
理して、プリメソフエーズ炭素質を含むピツチ状物質の
全部を実質的に光学的に異方性のメソフエーズ炭素質に
変換させる方法(特開昭58−18421)及びメソフ
エーズピツチに存在する多環多核の炭化水素が部分的に
水素化された構造の、実質的にキノリン可溶性多環多核
骨格の炭化水素を潜在的異方性形成成分として含有し、
溶融状態ではメソフエーズを実質的に形成しないで、全
体的に均質でかつ光学的に等方性の単一相を形成し、外
力を加えるとその方向への配向性を示す、H/Cが0.55
〜1.2の潜在的異方性ピツチ(特開昭57−10018
6)が報告されている。しかし、いずれの水添処理が必
須とされている。また前者の場合、プリメソフエーズピ
ツチすなわちキノリン可溶なピツチ単独による炭素繊維
製造の実施例がなく、紡糸用ピツチはキノリン不溶分を
含有するものとなつている。
For example, a pitch-like substance mainly composed of optically isotropic premesophase carbonaceous material or optically isotropic premesophase carbonaceous material is spun under the condition that the mesophase carbon mass is not substantially increased, and then subjected to infusibilization treatment. Then, a method of converting all of the pitch-like substance containing the premesophase carbonaceous material into a substantially optically anisotropic mesophase carbonaceous material by carbonization treatment (Japanese Patent Application Laid-Open No. 58-18421) and a method present in the mesophase pitch. Containing a hydrocarbon of a substantially quinoline-soluble polycyclic polynuclear skeleton having a structure in which the polycyclic polynuclear hydrocarbon is partially hydrogenated, as a potential anisotropy-forming component,
In the molten state, mesophase is not substantially formed, and a homogeneous and optically isotropic single phase is formed, and when an external force is applied, it exhibits orientation in that direction. H / C is 0.55.
To 1.2 latent anisotropic pitch (JP-A-57-10018)
6) has been reported. However, any hydrogenation treatment is required. Further, in the former case, there is no example of carbon fiber production using only primomethaze pitch, that is, quinoline-soluble pitch alone, and the spinning pitch contains quinoline-insoluble matter.

更に、コールタール、コールタールピツチ、石油系重質
油、石油の常圧残留油、減圧蒸留及びこれらの残油の熱
処理によつて副生するタールやピツチ、オイルサンド又
はビチユーメンの原料に水素化溶媒を添加して300〜
500℃に10〜60分間加熱し、次いで減圧下で45
0℃以上の温度に5〜60分間加熱してプリメソフエー
ズ含有ピツチを作り、得られた紡糸用ピツチを粘性変化
温度よりも高い温度まで昇温した後、紡糸し、急冷した
後250〜350℃の温度で不融化処理し、不融化処理
された繊維を不活性ガス中で1000〜1500℃の温
度に加熱することによつて製造される。X線回折より求
めた配向角が30〜50°、結晶サイズ(Lc)が12
〜80Å、層間隔(d002)が3.4〜3.6Åで、引張強
度が少なくとも200kgf/mm2、モジユラスが1000
0kgf/mm2であるピツチ系炭素繊維が報告されている
(特開昭59−53717)。
In addition, coal tar, coal tar pitches, heavy petroleum oils, residual oil of petroleum at atmospheric pressure, distillation under reduced pressure, and hydrogenation of tar and pits, oil sands or raw materials produced by heat treatment of these residual oils as raw materials. 300 ~ by adding solvent
Heat to 500 ° C for 10-60 minutes, then under reduced pressure 45
A premesophase-containing pitch is heated to a temperature of 0 ° C. or higher for 5 to 60 minutes, the obtained spinning pitch is heated to a temperature higher than the viscosity change temperature, spun, and rapidly cooled, and then heated at 250 to 350 ° C. It is produced by infusibilizing at a temperature and heating the infusibilized fiber to a temperature of 1000 to 1500 ° C. in an inert gas. The orientation angle determined by X-ray diffraction is 30 to 50 °, and the crystal size (Lc) is 12.
~ 80Å, layer spacing (d 002 ) is 3.4-3.6Å, tensile strength is at least 200 kgf / mm 2 , and module is 1000.
Pitch-based carbon fibers having a weight of 0 kgf / mm 2 have been reported (JP-A-59-53717).

特に、配向角が30°より小さく微結晶の見掛けの大き
さが80Åよりも大きい多結晶黒鉛の三次元構造を有し
ているメソフエーズピツチ系炭素繊維は、高い熱伝導性
及び電気伝導性を示すが、繊維としての機械特性がPA
N系炭素繊維に劣つていると報告されている。
In particular, the mesophase pitch-based carbon fiber having a three-dimensional structure of polycrystalline graphite having an orientation angle of less than 30 ° and an apparent size of microcrystals of more than 80Å has high thermal conductivity and electrical conductivity. Shows that the mechanical properties of the fiber are PA
It is reported to be inferior to N-based carbon fibers.

一般に、炭素繊維の機械的特性は、高次構造に支配され
る。例えば、高い弾性率は繊維構造を有し、且つ高い配
向性を持つていることが不可欠である。従来、高弾性の
ピツチ系炭素繊維を作るためには、紡糸用原料ピツチと
してコールタール、コールタールピツチ等の原料を加熱
重合し、次いで晶質化したメソフエーズピツチ、あるい
は潜在的異方性ピツチ又はプリメソフエーズピツチを用
いることが必要であつた。
Generally, the mechanical properties of carbon fibers are dominated by higher order structures. For example, it is essential that the high elastic modulus has a fiber structure and has a high orientation. Conventionally, in order to produce highly elastic Pitch-based carbon fiber, raw materials such as coal tar and coal tar pitch are heat-polymerized as a raw material pitch for spinning and then crystallized mesophase pitch, or latent anisotropy. It was necessary to use a pitch or prime mesophase pitch.

上述した方法によるピツチ系炭素繊維は、いずれもPA
N系炭素繊維に比較して黒鉛化特性は優れているが、繊
維としての引張強さにおいてはまだ劣つており、PAN
系炭素繊維と同等の機械特性を有するピツチ系炭素繊維
を提供するまでに到つていないのが実情である。
The Pitch-based carbon fibers produced by the above-mentioned method are all PA
The graphitization property is superior to N-based carbon fiber, but it is still inferior in tensile strength as a fiber.
The reality is that a Pitch-based carbon fiber having mechanical characteristics equivalent to those of the carbon-based carbon fiber has not yet been provided.

本発明者らは、引張強さ、引張弾性率及び破断伸びなど
の機械的特性において、PAN系炭素繊維に匹敵する
か、またはそれ以上に優れたピツチ系炭素繊維を開発す
るために鋭意研究を行なつた結果、ナフタリンを原料と
して特定の条件下で加熱重合し、軽質分を除去して得た
均質で適当な分子構造と分子量を有する光学的等方性ピ
ツチを紡糸原料ピツチとして用いて、紡糸、不融化、炭
化焼成及び高温処理することにより得られるピツチ系炭
素繊維は、配向角が30°未満であり且つ微結晶の見掛
けの大きさが80Åよりも大きく、更に驚くべきこと
に、炭素網面が選択的に繊維軸方向に配列した繊維構造
が賦与されているにもかかわらず、従来のメンソフエー
ズピツチ系黒鉛化繊維に特有の三次元構造を有すること
なく、その結果としてPAN系炭素繊維に匹敵する高強
度、高弾性率の機械的特性を有することを見出し、この
知見に基づいて本発明を成すに至つた。
The inventors of the present invention have conducted diligent research to develop a Pitch-based carbon fiber which is equal to or better than the PAN-based carbon fiber in mechanical properties such as tensile strength, tensile modulus and elongation at break. As a result of conducting, heat polymerization under specific conditions using naphthalene as a raw material, using a homogeneous and optically isotropic pitch having a suitable molecular structure and molecular weight obtained by removing light components as a spinning raw material pitch, Pitch-based carbon fibers obtained by spinning, infusibilizing, carbonizing and firing, and high-temperature treatment have an orientation angle of less than 30 ° and an apparent size of microcrystals larger than 80Å. Despite the fiber structure in which the mesh surface is selectively arranged in the fiber axis direction, it does not have the three-dimensional structure peculiar to the conventional Mensophase pitch-based graphitized fiber, and as a result, High strength comparable to AN-based carbon fiber, found to have mechanical properties of high modulus, ItaruTsuta the present invention based on this finding.

すなわち、本発明は、X線回折により求めた配向角(2
Z°)が30°未満であり、微結晶の見掛けの大きさ
(Lc(002))が80Åを超え且つ200Å以下で
あり、層間隔(d002)が3.371〜3.440Åを示すナフ
タリンを原料として2000℃以上で処理されたピツチ
系炭素繊維を提供することをその目的としている。本発
明の他の目的は、ナフタリンをルイス酸触媒の存在下で
330℃以下で0.5〜100時間加熱重合し、触媒を除
去した後、常圧下又は減圧下不活性ガスを流通しながら
330〜440℃に加熱して軽質分を除去し、軟化点が
180〜200℃で、H/Cが0.6〜0.8、平均分子量が
800〜1500、ベンゼン不溶分が35〜45重量%
であり且つキノリン不溶分を含んでいない光学的等方性
の炭素質ピツチを生成し、生成した炭素質ピツチを常法
により紡糸、不融化及び炭化焼成した後、2000℃以
上の温度で且つ不活性ガス雰囲気下で処理することによ
る、上述の特性を有するピツチ系炭素繊維の製造方法を
提供することである。
That is, in the present invention, the orientation angle (2
Z °) is less than 30 °, the apparent size (Lc (002) ) of the microcrystals is more than 80 Å and 200 Å or less, and the layer interval (d 002 ) is 3.371 to 3.440 Å using naphthalene as a raw material. It is an object of the present invention to provide a Pitch-based carbon fiber treated at 2000 ° C or higher. Another object of the present invention is to heat-polymerize naphthalene at 330 ° C. or lower for 0.5 to 100 hours in the presence of a Lewis acid catalyst, remove the catalyst, and then pass 330 to 440 while flowing an inert gas under normal pressure or reduced pressure. Light weight is removed by heating to ℃, softening point is 180 ~ 200 ℃, H / C is 0.6 ~ 0.8, average molecular weight is 800 ~ 1500, benzene insoluble is 35 ~ 45wt%.
And an optically isotropic carbonaceous pitch containing no quinoline insoluble matter is formed, and the produced carbonaceous pitch is spun, infusibilized and carbonized by a conventional method, and then heated at a temperature of 2000 ° C. or higher and It is an object of the present invention to provide a method for producing a Pitch-based carbon fiber having the above-mentioned characteristics by treating in an active gas atmosphere.

本発明の炭素繊維は、X線回折により求められる配向角
(2Z°)が30°未満、好しくは15〜25°であ
り、微結晶の見掛けの大きさ(Lc(002))が80
Åを超え且つ200Å以下、好しくは90〜170Åで
あり、層間隔(d002)が3.371〜3.440Å、好しくは
3.390〜3.430Åである。
The carbon fiber of the present invention has an orientation angle (2Z °) determined by X-ray diffraction of less than 30 °, preferably 15 to 25 °, and an apparent size (Lc (002) ) of microcrystals of 80.
It is more than Å and less than 200 Å, preferably 90 to 170 Å, and the layer interval (d 002 ) is 3.371 to 3.440 Å, preferably
3.390 to 3.430Å.

上述したような配向角、微結晶の見掛けの大きさ及び層
間隔を有し、結晶が均質に配列している構造を有する本
発明の炭素繊維は従来のピツチ系炭素繊維よりも優れた
機械的強さを示すものである。
The carbon fiber of the present invention having the orientation angle, the apparent size of microcrystals and the layer spacing as described above, and the structure in which the crystals are uniformly arranged is superior in mechanical strength to the conventional Pitch-based carbon fiber. It shows the strength.

本発明の炭素繊維は、少なくとも300kgf/mm2の引張
強さと、少なくとも20000kgf/mm2の引張弾性率を
有している。
Carbon fiber of the present invention has a tensile strength of at least 300 kgf / mm 2, at least a tensile modulus of 20,000 kgf / mm 2.

ナフタリンを原料として特定の方法で製造された光学的
等方性の炭素質ピツチは、メソフエーズピツチの紡糸温
度と比較して、より低温で溶融紡糸が可能であり、紡糸
時に特定の紡糸条件を採用することなく、均質なピツチ
繊維を得ることができる。更に、ピツチ繊維の基本配列
がメソフエーズピツチから得られるピツチ繊維程、強固
でないため、不融化の際、表層部で不融化反応が進むこ
とによつて、微細なモザイク状組織が形成され、中心部
では不融化反応によつて分子の好ましい配列が乱される
ことなく優れた繊維構造が賦与される。
Optically isotropic carbonaceous pitch produced by a specific method using naphthalene as raw material, compared with the spinning temperature of the mesophase pitch, melt spinning is possible at a lower temperature, and specific spinning conditions during spinning. It is possible to obtain a uniform pitch fiber without adopting. Furthermore, since the basic arrangement of the Pitch fibers is not as strong as the Pitch fibers obtained from the mesophase pitch, the infusibilization reaction proceeds in the surface layer during infusibilization, whereby a fine mosaic structure is formed, In the central part, an excellent fiber structure is provided without disturbing the preferable arrangement of molecules by the infusible reaction.

次に、本発明の製造方法について説明する。Next, the manufacturing method of the present invention will be described.

原料であるナフタリンをルイス酸触媒の存在下で330
℃以下、好ましくは100〜300℃に0.5〜100時
間加熱して重合する。
The raw material naphthalene was added in the presence of a Lewis acid catalyst for 330
Polymerization is carried out by heating at a temperature of not higher than 0.degree.

ここで使用するルイス酸触媒としては、AlCl3,BF3等を
例示し得るが、AlCl3が好ましい。ルイス酸触媒はナフ
タリン100重量部に対して5〜50重量部使用し得る
が8〜20重量部が好ましい。尚、加熱温度が330℃
を超えると、メソフエーズピツチが生成するため、キノ
リン不溶分が存在するようになるので好しくない。また
ルイス酸触媒を50重量部以上用いても、重合効率はあ
まり変らず且つ触媒の除去などが煩雑となり、経済的で
はない。
Examples of the Lewis acid catalyst used here include AlCl 3 and BF 3, but AlCl 3 is preferable. The Lewis acid catalyst may be used in an amount of 5 to 50 parts by weight, preferably 8 to 20 parts by weight, based on 100 parts by weight of naphthalene. The heating temperature is 330 ℃
Above this, mesophase pitch will be formed, and quinoline insoluble matter will be present, which is not preferable. Even if 50 parts by weight or more of the Lewis acid catalyst is used, the polymerization efficiency does not change so much and the removal of the catalyst becomes complicated, which is not economical.

重合されたナフタリンから触媒を除去した後、常圧下又
は減圧下不活性ガスを流通しながら330〜440℃、
好ましくは350〜420℃に加熱して軽質分を除去
し、光学的に等方性の炭素質ピツチを製造する。加熱温
度が440℃を超えると、メソフエーズピツチが生成
し、キノリン不溶分が存在するようになるので好ましく
ない。
After removing the catalyst from the polymerized naphthalene, 330 to 440 ° C. while flowing an inert gas under normal pressure or reduced pressure,
Preferably, it is heated to 350 to 420 ° C. to remove light components to produce an optically isotropic carbonaceous pitch. If the heating temperature exceeds 440 ° C., mesophase pitch is generated and quinoline insoluble matter is present, which is not preferable.

かようにして得られた炭素質ピツチ(紡糸原料ピツチ)
は、軟化点が180〜200℃で、H/Cが0.6〜0.8、
平均分子量が800〜1500、ベンゼン不溶分が35
〜45重量%であり、且つキノリン不溶分を含有せず且
つ偏光顕微鏡によつて観察すると等方性を示す。
Carbonaceous pitch thus obtained (spinning raw material pitch)
Has a softening point of 180 to 200 ° C., H / C of 0.6 to 0.8,
Average molecular weight is 800-1500, benzene insoluble matter is 35
˜45% by weight, containing no quinoline insoluble matter, and exhibiting isotropicity when observed by a polarizing microscope.

本発明の優れた機械特性を有する炭素繊維を製造するた
めの紡糸原料ピツチとしては、上述の諸性質を満足する
炭素質ピツチであることが必要である。
The spinning raw material pitch for producing the carbon fiber having excellent mechanical properties of the present invention is required to be a carbonaceous pitch satisfying the above-mentioned various properties.

得られた炭素質ピツチを常法により紡糸及び不融化処理
する。例えば、紡糸は、紡糸口金から吐出する時の炭素
質ピツチの温度を炭素質ピツチの軟化点よりも70〜9
0℃高い温度に設定して、0.5〜2.0kgf/cm2・Gの圧力を
かけて吐出し、300〜1000m/分の捲取り速度で捲取る
ことによつておこなわれる。また不融化処理は、酸化性
ガス雰囲気下で、0.5〜5℃/分の昇温速度で230〜
300℃まで加熱し、そのまま30〜60分間維持する
ことによつて不融化処理される。
The obtained carbonaceous pitch is spun and infusibilized by a conventional method. For example, in spinning, the temperature of the carbonaceous pitch at the time of discharging from the spinneret is 70 to 9 above the softening point of the carbonaceous pitch.
It is carried out by setting the temperature at 0 ° C. higher, discharging under a pressure of 0.5 to 2.0 kgf / cm 2 · G, and winding at a winding speed of 300 to 1000 m / min. In addition, the infusibilizing treatment is performed in an oxidizing gas atmosphere at a temperature rising rate of 0.5 to 5 ° C./min for 230 to
It is infusibilized by heating to 300 ° C. and maintaining it for 30 to 60 minutes.

このように不融化処理した繊維は、次に不活性ガス、例
えばN2ガス中で、5〜15℃/分の昇温速度で900
℃まで加熱し、次いで例えばアルゴンガス中で2000
℃以上の所定の温度で処理することにより高い炭化収率
で炭素繊維を得ることができる。
The fiber thus infusibilized is then heated in an inert gas such as N 2 gas at a temperature rising rate of 5 to 15 ° C./min to 900
Heated to 0 ° C., then 2000 for example in argon gas
By treating at a predetermined temperature of ℃ or more, it is possible to obtain carbon fibers with a high carbonization yield.

次に、本発明における繊維及びピツチの特性を表わす各
指標について説明する。
Next, each index representing the characteristics of the fiber and the pitch in the present invention will be described.

(1)構造関連因子 配向角(2Z°)、微結晶のC軸方向の見掛けの大きさ
(Lc)及び層間隔(d002)は広角X線回折図形か
ら求められる繊維の高次構造を表わす構造関連因子であ
る。配向角(2Z°)は微結晶の繊維軸方向に対する配
向の程度を示すもので、この角度が小さい程配向が進ん
でいることを意味する。微結晶の見掛けの大きさ(L
c)は炭素微結晶の見掛けの積層高さを表わし、層間隔
(d002)は微結晶の炭素網面間の面間隔を表わす。
(1) Structure-related factors The orientation angle (2Z °), the apparent size of the crystallites in the C-axis direction (Lc), and the layer spacing (d 002 ) represent the higher-order structure of the fiber obtained from the wide-angle X-ray diffraction pattern. It is a structure-related factor. The orientation angle (2Z °) indicates the degree of orientation of the crystallites with respect to the fiber axis direction, and the smaller this angle, the more the orientation advances. Apparent size of microcrystal (L
c) represents the apparent stacking height of the carbon microcrystals, and the layer spacing (d 002 ) represents the interplanar spacing between the carbon network planes of the microcrystals.

微結晶の見掛けの大きさ(Lc)の測定は学振法(日本
学術振興会第117委員会、炭素、No.36、5,196
3)による。
The apparent size (Lc) of the microcrystal is measured by the Gakshin method (Japan Society for the Promotion of Science 117th Committee, Carbon, No.36, 5,196).
According to 3).

配向角(2Z°)は(002)回折強度の最大値を示す回折
角の位置において構成繊維を平行に揃えた繊維束をX線
ビームの垂直面内において180°回転することによ
り、(002)回折環にそつてその強度分布を測定し、強度
最大値の1/2の点における半価幅として規定する。
The orientation angle (2Z °) is (002). By rotating the fiber bundle in which the constituent fibers are aligned in parallel at the position of the diffraction angle showing the maximum value of the diffraction intensity by 180 ° in the vertical plane of the X-ray beam, (002) The intensity distribution is measured along the diffraction ring and is defined as the half width at half the intensity maximum.

(2)ピツチの特性を示すパラメーター a)分子量 ピリジンを溶媒として、蒸気圧オスモメーター(VP
O)を使用して測定する。VPOとしては、(コロナ製
117型分子量測定装置)を用い、溶媒としてピリジ
ン、標準物質としてベンジルを使用する。
(2) Parameters indicating the characteristics of pitch a) Molecular weight Using pyridine as a solvent, vapor pressure osmometer (VP
O) is used for measurement. As VPO, (Model 117 molecular weight measuring device manufactured by Corona) is used, and pyridine is used as a solvent and benzyl is used as a standard substance.

b)H/C JIS M−8813に従つて測定した元素分析により
次式に従つて算出する。
b) Calculated according to the following formula by elemental analysis measured according to H / C JIS M-8813.

c)軟化点 高化式フローテスタ(島津製作所)を用い、加熱体セル
(内径10mm、ノズル径1mm)に100メツシユ以下に
粉砕したピツチを1g入れ、上部より10kgf/cm2の荷
重をかけ、昇温速度6℃/分で昇温し可塑化曲線の変曲
点の温度をもつて軟化点とする。
c) Softening point Using a Koka flow tester (Shimadzu Corporation), put 1 g of crushed pitch of 100 mesh or less into a heating cell (inner diameter 10 mm, nozzle diameter 1 mm) and apply a load of 10 kgf / cm 2 from the top. The temperature is raised at a temperature rising rate of 6 ° C./min, and the temperature at the inflection point of the plasticization curve is taken as the softening point.

d)溶剤不溶分 JIS−K−2425に準拠して測定し
た。
d) Solvent insoluble matter It measured based on JIS-K-2425.

(3)炭素繊維の物性 炭素繊維の繊維直径、引張強さ、伸び、引張弾性率はJ
IS R−7601「炭素繊維試験方法」に従つて測定
する。尚、繊維直径の測定は断面積法を採用する。
(3) Physical properties of carbon fiber The fiber diameter, tensile strength, elongation and tensile modulus of carbon fiber are J
It is measured according to ISR-7601 "Carbon fiber test method". The fiber diameter is measured by the cross-sectional area method.

以下、実施例を挙げて本発明を説明する。尚、これらの
実施例は単に例示的なもので、本発明を限定するもので
はないことを付言する。
Hereinafter, the present invention will be described with reference to examples. It should be noted that these examples are merely illustrative and do not limit the present invention.

実施例1 ナフタリン(関東化学株式会社製 1級試薬)1000
gと触媒としてAlCl3(関東化学株式会社製 1級試
薬)100gを攪拌機付ガラス製三口フラスコに仕込
み、210℃、60時間重合した。重合終了後触媒除去
のため水洗、ロ過(孔径0.2μm)を行いピツチを得
た。得られたピツチを400℃,15Torr、15分間N
2流通下で加熱して軽質分を除去した。
Example 1 Naphthalene (first-class reagent manufactured by Kanto Chemical Co., Inc.) 1000
g and 100 g of AlCl 3 (first-class reagent manufactured by Kanto Chemical Co., Inc.) as a catalyst were charged in a glass three-necked flask equipped with a stirrer and polymerized at 210 ° C. for 60 hours. After completion of the polymerization, the catalyst was removed by washing with water and filtration (pore size 0.2 μm) to obtain a pitch. The obtained pitch is 400 ° C, 15 Torr, N for 15 minutes
2 Heated under circulation to remove light components.

かようにして得られた炭素質ピツチは、偏光顕微鏡下で
観察したところ光学的に等方性であり、かつその特性は
第1表の通りである。
The carbonaceous pits thus obtained are optically isotropic when observed under a polarizing microscope, and their characteristics are as shown in Table 1.

次に炭素質ピツチを口径0.3mmのノズルをもつシリンダ
ーに入れ、280℃に加熱溶融し、次いで1.2kgf/cm2G
のN2ガス圧にて、上記ノズルを通して押出し紡糸し
た。この時の捲取速度は約700m/分であつた。上述
のようにして得られたピツチ繊維は空気雰囲気下で、約
1℃/分の昇温速度で、265℃まで加熱し、この雰囲
気下でピツチ繊維を約30分間保持して不融化処理し
た。
Next, the carbonaceous pitch is put into a cylinder with a nozzle having a diameter of 0.3 mm, heated and melted at 280 ° C., and then 1.2 kgf / cm 2 G
Extruded and spun through the nozzle at N 2 gas pressure of. The winding speed at this time was about 700 m / min. The pitch fibers obtained as described above were heated to 265 ° C. at a temperature rising rate of about 1 ° C./min in an air atmosphere, and the pitch fibers were held in this atmosphere for about 30 minutes to be infusibilized. .

このように不融化処理された繊維をN2ガス雰囲気下
で、約5℃/分の昇温速度で900まで加熱し、次いで
約50℃/分の昇温速度でアルゴン雰囲気下で2000
℃まで加熱し、この雰囲気中で約10分間保持し処理し
た。
The fibers thus infusibilized are heated in an N 2 gas atmosphere at a heating rate of about 5 ° C./min to 900, and then at a heating rate of about 50 ° C./min in an argon atmosphere at 2000.
The sample was heated to 0 ° C. and kept in this atmosphere for about 10 minutes for processing.

得られた炭素繊維(直径:8μm)のX線回折により求
めた物性及び機械的特性を第2表に示す。
Table 2 shows the physical properties and mechanical properties of the obtained carbon fiber (diameter: 8 μm) determined by X-ray diffraction.

実施例2 実施例1で得られた炭素繊維を更にアルゴンガス雰囲気
下で約50℃/分の昇温速度で2500℃まで加熱し
て、この温度で約10分間保持し処理した。
Example 2 The carbon fiber obtained in Example 1 was further heated in an argon gas atmosphere to 2500 ° C. at a temperature rising rate of about 50 ° C./min, and held at this temperature for about 10 minutes for treatment.

得られた炭素繊維の(直径:7.5μm)X線回折により
求めた物性及び機械的特性を第3表に示す。
Table 3 shows the physical properties and mechanical properties of the obtained carbon fiber determined by X-ray diffraction (diameter: 7.5 μm).

実施例3 実施例1で得られた炭素繊維を更にアルゴンガス雰囲気
下で約50℃の昇温速度で2800℃まで加熱し、この
温度で約10分間保持し処理した。得られた炭素繊維
(直径:7.5μm)のX線回折により求めた物性及び機
械的特性を第4表に示す。
Example 3 The carbon fiber obtained in Example 1 was further heated to 2800 ° C. at a temperature rising rate of about 50 ° C. in an argon gas atmosphere, and kept at this temperature for about 10 minutes for treatment. Table 4 shows the physical properties and mechanical properties of the obtained carbon fiber (diameter: 7.5 μm) determined by X-ray diffraction.

実施例4 ナフタリン(関東化学株式会社製 1級試薬)1000
gと触媒としてAlCl3(関東化学株式会社製 1級試
薬)100gを磁石誘導攪拌装置を備えたオートクレー
ブに仕込み、密閉後、N2ガスで充分置換後、内圧0kg
f/cm2Gとし、攪拌をしながら300℃まで昇温し、30
0℃で1時間重合させた。重合終了後、触媒除去のため
水洗、ロ過(孔径0.2μm)を行いピツチを得た。得ら
れたピツチを350℃,12Torr、30分間N2ガス流
通下で加熱して軽質分を除去した。
Example 4 Naphthalene (Kanto Chemical Co., Inc. first-grade reagent) 1000
g and 100 g of AlCl 3 (Kanto Chemical Co., Ltd. first-class reagent) as a catalyst were charged into an autoclave equipped with a magnet induction stirrer, sealed, and sufficiently replaced with N 2 gas, and the internal pressure was 0 kg.
f / cm 2 G, raise the temperature to 300 ° C with stirring, and
Polymerization was carried out at 0 ° C. for 1 hour. After completion of the polymerization, the catalyst was removed by washing with water and filtration (pore size 0.2 μm) to obtain a pitch. The obtained pitch was heated at 350 ° C., 12 Torr for 30 minutes under N 2 gas flow to remove light components.

かようにして得られた炭素質ピツチは、偏光顕微鏡で観
察したところ光学的等方性でありかつその特性は第5表
の通りである。
The carbonaceous pits thus obtained are optically isotropic when observed with a polarizing microscope, and their characteristics are as shown in Table 5.

次に炭素質ピツチを口径0.3mmのノズルをもつシリンダ
ーに入れ275℃に加熱、溶融し次いで0.8kgf/cm2Gの
N2ガス圧にて、上記のノズルを通して押出し紡糸し
た。この時の捲取速度は約600m/分であつた。上述
のようにして得られたピツチ繊維は空気雰囲気下で約1
℃/分の昇温速度で250℃まで加熱し、この雰囲気中
でピツチ繊維を約30分間保持して不融化処理した。
Next, the carbonaceous pitch was placed in a cylinder having a nozzle having a diameter of 0.3 mm, heated to 275 ° C., melted, and then extruded and spun through the above nozzle at a N 2 gas pressure of 0.8 kgf / cm 2 G. The winding speed at this time was about 600 m / min. The pitch fibers obtained as described above are about 1 in air atmosphere.
The pitch fibers were heated to 250 ° C. at a temperature rising rate of ° C./min, and the pitch fibers were held in this atmosphere for about 30 minutes for infusibilization treatment.

このように不融化処理された繊維をN2ガス雰囲気下
で、約5℃/分の昇温速度で900℃まで加熱し、次い
で、約50℃/分の昇温速度でアルゴンガス雰囲気下で
2000℃まで加熱し、この雰囲気中で約10分間保持
し処理した。
The fibers thus infusibilized are heated in an N 2 gas atmosphere to 900 ° C. at a heating rate of about 5 ° C./minute, and then under an argon gas atmosphere at a heating rate of about 50 ° C./minute. The sample was heated to 2000 ° C. and kept in this atmosphere for about 10 minutes for processing.

得られた炭素繊維(直径:7.5μm)のX線回折により
求めた物性及び機械的特性を第6表に示す。
Table 6 shows the physical properties and mechanical properties of the obtained carbon fiber (diameter: 7.5 μm) determined by X-ray diffraction.

実施例5 実施例4で得られた炭素繊維を更にアルゴンガス雰囲気
下で約50℃/分の昇温速度で2500℃まで加熱し
て、この雰囲気中で約10分間保持し処理した。
Example 5 The carbon fiber obtained in Example 4 was further heated in an argon gas atmosphere to 2500 ° C. at a temperature rising rate of about 50 ° C./min, and held in this atmosphere for about 10 minutes for treatment.

得られた炭素繊維(直径:7.5μm)のX線回折より求
めた物性及び機械的特性を第7表に示す。
Table 7 shows the physical properties and mechanical properties of the obtained carbon fiber (diameter: 7.5 μm) determined by X-ray diffraction.

実施例6 実施例4で得られた炭素繊維を更にアルゴンガス雰囲気
下で約50℃/分の昇温速度で約2800℃まで加熱し
て、この雰囲気中で約10分間保持し処理した。
Example 6 The carbon fiber obtained in Example 4 was further heated in an argon gas atmosphere to about 2800 ° C. at a temperature rising rate of about 50 ° C./min, and held in this atmosphere for about 10 minutes for treatment.

得られた炭素繊維(直径:7μm)のX線回折により求
めた物性及び機械的特性を第8表に示す。
Table 8 shows the physical properties and mechanical properties of the obtained carbon fiber (diameter: 7 μm) determined by X-ray diffraction.

実施例7 ナフタリン(関東化学株式会社製1級試薬)1000g
と触媒としてAlCl3(関東化学株式会社製1級試薬)1
00gを撹拌機付き三口フラスコに仕込み、100℃、
60時間重合した。次いで触媒のAlCl3(関東化学株式
会社製1級試薬)100gを更に加え、210℃、30
時間重合した。重合終了後、触媒辞去のため水洗ロ過
(孔径0.2μm)を行いピツチを得た。
Example 7 1000 g of naphthalene (first-class reagent manufactured by Kanto Chemical Co., Inc.)
And AlCl 3 as a catalyst (Kanto Chemical Co., Ltd. first-grade reagent) 1
Charge 00g into a three-necked flask equipped with a stirrer,
Polymerization was carried out for 60 hours. Next, 100 g of AlCl 3 (first-class reagent manufactured by Kanto Kagaku Co., Ltd.) as a catalyst was further added, and the temperature was maintained at 210 ° C.
Polymerized for hours. After the completion of the polymerization, the catalyst was removed by washing with water (pore size: 0.2 μm) to obtain a pitch.

得られたピツチを380℃、10Torr20分間N2ガス
流通下で加熱して軽質分を除去した。
The obtained pitch was heated at 380 ° C. for 10 Torr for 20 minutes under N 2 gas flow to remove light components.

かようにして得られた炭素質ピツチは、偏光顕微鏡下で
観察したところ光学的に等方性であり、かつその特性は
第9表の通りである。
The carbonaceous pits thus obtained are optically isotropic when observed under a polarizing microscope, and their characteristics are as shown in Table 9.

次に炭素質ピツチを口径0.3mmのノズルをもつシリンダ
ーに入れ275℃に加熱溶融し、次いで1.2kgf/cm2Gの
N2ガス圧にて上記ノズルを通して、押出し紡糸した。
この時の捲取速度は、約500m/分であつた。
Next, the carbonaceous pitch was placed in a cylinder having a nozzle having a diameter of 0.3 mm, heated and melted at 275 ° C., and then extrusion spun through the nozzle at a N 2 gas pressure of 1.2 kgf / cm 2 G.
The winding speed at this time was about 500 m / min.

上述のように得られたピツチ繊維は空気雰囲気下で約1
℃/分の昇温速度で265℃まで加熱しこの雰囲気下で
ピツチ繊維を約30分間保持して不融化処理した。
The pitch fibers obtained as described above are about 1 in air atmosphere.
The pitch fibers were heated to 265 ° C. at a temperature rising rate of ° C./min, and the pitch fibers were held in this atmosphere for about 30 minutes for infusibilization.

このように不融化処理された繊維をN2ガス雰囲気下で
約5℃/分の昇温速度で900℃まで加熱し、次いで約
50℃/分の昇温速度で2000℃まで加熱し、この雰
囲気中で約10分間保持し処理した。
The infusibilized fiber was heated to 900 ° C. at a heating rate of about 5 ° C./min in an N 2 gas atmosphere, and then heated to 2000 ° C. at a heating rate of about 50 ° C./min. It was held in the atmosphere for about 10 minutes for processing.

得られた炭素繊維(直径:8μm)のX線回折により求
めた物性及び機械的特性を第10表に示す。
Table 10 shows the physical properties and mechanical properties of the obtained carbon fiber (diameter: 8 μm) determined by X-ray diffraction.

実施例8 実施例7で得られた炭素繊維を更に、アルゴンガス雰囲
気下で約50℃/分の昇温速度で2500℃まで加熱し
て、この雰囲気中で約10分間保持し処理した。
Example 8 The carbon fiber obtained in Example 7 was further heated to 2500 ° C. at a temperature rising rate of about 50 ° C./min in an argon gas atmosphere and held in this atmosphere for about 10 minutes for treatment.

得られた炭素繊維(直径:7.5μm)のX線回折により
求めた物性及び機械的特性を第11表に示す。
Table 11 shows the physical properties and mechanical properties of the obtained carbon fibers (diameter: 7.5 μm) determined by X-ray diffraction.

実施例9 実施例7で得られた炭素繊維を更にアルゴンガス雰囲気
下で約50℃/分の昇温速度で2800℃まで加熱し
て、この雰囲気下で約10分間保持し、処理した。
Example 9 The carbon fiber obtained in Example 7 was further heated to 2800 ° C. at a temperature rising rate of about 50 ° C./min in an argon gas atmosphere, and held in this atmosphere for about 10 minutes to be treated.

得られた炭素繊維(直径:7.5μm)のX線回折により
求めた物性及び機械的特性を第12表に示す。
Table 12 shows the physical properties and mechanical properties of the obtained carbon fiber (diameter: 7.5 μm) determined by X-ray diffraction.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】X線回折より求めた配向角(2Z°)が3
0°未満であり、微結晶の見掛けの大きさ(L
C(002))が80オングストロームを越え且つ20
0オングストローム以下であり、層間隔(d002)が
3.371−3.440オングストロームを示す、20
00℃以上の温度で処理されたナフタリンを原料とする
炭素繊維。
1. The orientation angle (2Z °) determined by X-ray diffraction is 3
It is less than 0 ° and the apparent size of the microcrystal (L
C (002) ) exceeds 80 angstroms and 20
20 Å or less and a layer spacing (d 002 ) of 3.371-3.440 Å, 20
Carbon fiber made from naphthalene treated at a temperature of 00 ° C or higher.
【請求項2】ナフタリンをルイス酸触媒の存在下330
℃以下で0.5−100時間加熱重合し、触媒を除去し
た後、常圧下又は減圧下不活性ガスを流通しながら33
0−440℃に加熱して軽質分を除去し、軟化点が18
0−200℃、H/Cが0.6−0.8、平均分子量が
800−1500、ベンゼン不溶分が35−45重量%
であり、且つキノリン不溶分を含んでいない光学的に等
方性なピッチを生成し、生成した等方性ピッチを紡糸、
不融化及び炭化焼成した後、2000℃以上の温度で処
理することを特徴とする、X線回折より求めた配向角
(2Z°)が30°未満であり、微結晶の見掛けの大き
さ(LC(002))が80オングストロームを越え且
つ200オングストローム以下であり、層間隔(d
002)が3.371−3.440オングストロームを
示す炭素繊維の製造方法。
2. Naphthalene in the presence of a Lewis acid catalyst 330
After heat-polymerization at 0.5 ° C. or less for 0.5 to 100 hours to remove the catalyst, under normal pressure or reduced pressure while passing an inert gas, 33
Heat to 0-440 ° C to remove light components, softening point 18
0-200 ° C, H / C 0.6-0.8, average molecular weight 800-1500, benzene insoluble content 35-45% by weight
And produce an optically isotropic pitch containing no quinoline insoluble matter, and spinning the produced isotropic pitch,
After being infusibilized and carbonized, it is treated at a temperature of 2000 ° C. or higher, the orientation angle (2Z °) determined by X-ray diffraction is less than 30 °, and the apparent size of the microcrystals (L C (002) ) is greater than 80 angstroms and less than 200 angstroms, and the layer spacing (d
002 ) is 3.371-3.440 angstroms.
JP59193247A 1984-09-14 1984-09-14 Carbon fiber and manufacturing method thereof Expired - Lifetime JPH0633530B2 (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
JP59193247A JPH0633530B2 (en) 1984-09-14 1984-09-14 Carbon fiber and manufacturing method thereof
CA000490155A CA1262007A (en) 1984-09-14 1985-09-06 Process for producing carbon fibers and the carbon fibers produced by the process
DE3546613A DE3546613C2 (en) 1984-09-14 1985-09-13
FR8513616A FR2570395B1 (en) 1984-09-14 1985-09-13 PROCESS FOR THE PREPARATION OF CARBON FIBERS AND CARBON FIBERS PRODUCED BY THIS PROCESS
GB08522741A GB2164351B (en) 1984-09-14 1985-09-13 Process for producing carbon fibers and pitch suitable for use therein
DE19853532785 DE3532785A1 (en) 1984-09-14 1985-09-13 METHOD FOR PRODUCING CARBON FIBERS AND CARBON FIBERS PRODUCED BY THIS METHOD
US07/293,563 US4863708A (en) 1984-09-14 1989-01-03 Process for producing carbon fibers and the carbon fibers produced by the process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59193247A JPH0633530B2 (en) 1984-09-14 1984-09-14 Carbon fiber and manufacturing method thereof

Publications (2)

Publication Number Publication Date
JPS6183319A JPS6183319A (en) 1986-04-26
JPH0633530B2 true JPH0633530B2 (en) 1994-05-02

Family

ID=16304777

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59193247A Expired - Lifetime JPH0633530B2 (en) 1984-09-14 1984-09-14 Carbon fiber and manufacturing method thereof

Country Status (1)

Country Link
JP (1) JPH0633530B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01118622A (en) * 1987-10-28 1989-05-11 Ube Ind Ltd High strength and high modulus carbon fiber
JPH0742615B2 (en) * 1988-03-28 1995-05-10 東燃料株式会社 High-strength, high-modulus pitch-based carbon fiber
JP2535207B2 (en) * 1988-06-30 1996-09-18 日本石油株式会社 Pitch-based carbon fiber having excellent compression properties and method for producing the same

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6057941B2 (en) * 1976-06-28 1985-12-17 エリツク・アラン・オルソン Method and apparatus for converting molten metal into solidified product
JPS5818421A (en) * 1981-07-27 1983-02-03 Agency Of Ind Science & Technol Preparation of carbon fiber
JPS5818613A (en) * 1981-07-28 1983-02-03 Olympus Optical Co Ltd Slanting light and dark visual field luminaire
US4431513A (en) * 1982-03-30 1984-02-14 Union Carbide Corporation Methods for producing mesophase pitch and binder pitch
JPS5953717A (en) * 1982-09-16 1984-03-28 Agency Of Ind Science & Technol Pitch-based carbon fiber having high strength and modulus and its manufacture

Also Published As

Publication number Publication date
JPS6183319A (en) 1986-04-26

Similar Documents

Publication Publication Date Title
Honda Carbonaceous mesophase: history and prospects
US4863708A (en) Process for producing carbon fibers and the carbon fibers produced by the process
KR910005574B1 (en) Process for producing pitch for carbon
JPS59196390A (en) Preparation of pitch for carbon fiber
JPS6327447B2 (en)
JPH0633528B2 (en) Carbon fiber and manufacturing method thereof
JP2780231B2 (en) Carbon fiber production method
JPH0633529B2 (en) Carbon fiber manufacturing method
JPS6183319A (en) Carbon fiber and its production
JPH0532494B2 (en)
JP2000319664A (en) Method for producing mesophase pitch and carbon fiber for carbon material
JPH0718057B2 (en) Pitch-based fiber manufacturing method
JPH0516475B2 (en)
JP2533487B2 (en) Carbon fiber manufacturing method
JPH0432118B2 (en)
JPH0316403B2 (en)
JP3016089B2 (en) Ultra-low softening point, low viscosity mesophase pitch, method for producing the same, and method for producing high-strength, high-modulus carbon fiber
WO2024181365A1 (en) Mesophase pitch for carbon fiber and method for producing mesophase-pitch-based carbon fiber
JP3055295B2 (en) Pitch-based carbon fiber and method for producing the same
JPS59184287A (en) Preparation of spun pitch for carbon fiber
JPH0739580B2 (en) Method for producing spinning pitch for carbon fiber
JP2594907B2 (en) Method for producing pitch carbon fiber
JP2982406B2 (en) Method for producing spinning pitch for carbon fiber
JPS61258024A (en) Production of pitch carbon yarn
JPH0148315B2 (en)