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JPH0633528B2 - Carbon fiber and manufacturing method thereof - Google Patents
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JPH0633528B2 - Carbon fiber and manufacturing method thereof - Google Patents

Carbon fiber and manufacturing method thereof

Info

Publication number
JPH0633528B2
JPH0633528B2 JP59193245A JP19324584A JPH0633528B2 JP H0633528 B2 JPH0633528 B2 JP H0633528B2 JP 59193245 A JP59193245 A JP 59193245A JP 19324584 A JP19324584 A JP 19324584A JP H0633528 B2 JPH0633528 B2 JP H0633528B2
Authority
JP
Japan
Prior art keywords
pitch
carbon fiber
fiber
temperature
naphthalene
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
JP59193245A
Other languages
Japanese (ja)
Other versions
JPS6183317A (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 JP59193245A priority Critical patent/JPH0633528B2/en
Priority to CA000490155A priority patent/CA1262007A/en
Priority to FR8513616A priority patent/FR2570395B1/en
Priority to DE3546613A priority patent/DE3546613C2/de
Priority to DE19853532785 priority patent/DE3532785A1/en
Priority to GB08522741A priority patent/GB2164351B/en
Publication of JPS6183317A publication Critical patent/JPS6183317A/en
Priority to US07/293,563 priority patent/US4863708A/en
Publication of JPH0633528B2 publication Critical patent/JPH0633528B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Inorganic Fibers (AREA)

Description

【発明の詳細な説明】 本発明は、ナフタリンを原料とする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。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a novel Pitch-based carbon fiber made of naphthalene as a raw material and a method for producing the same.

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。
Currently available carbon fiber is polyacrylonitrile.
PAN-based carbon fibers made from (PAN) and Pitch-based carbon fibers made from Pitches are classified according to the raw materials.Generally, PAN-based carbon fibers are compared to Pitch-based carbon fibers. In particular, PAN-based carbon fiber has been the mainstream as a high-performance carbon fiber having high strength and high elastic modulus because it has excellent properties especially in terms of tensile strength. However, since PAN-based carbon fiber is expensive and has a low carbonization yield, it is possible to obtain the same tensile strength and tensile modulus as PAN-based carbon fiber by using Pitch, which is advantageous in terms of economy, as a 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%のメソ相が生ずるのに十分な時間加熱し、紡糸温度
で非チキソトロピー性で、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
雰囲気中で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、すなわち硬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100
0Å以上の見掛け積層高さ(Lc)を有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49-19127)。
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 mesophases, non-thixotropic at spinning temperatures, A carbonaceous pitch having a viscosity of 200 poise is spun, the spun fiber is made infusible at 250 to 400 ° C. in an oxygen-containing atmosphere, and the infusible fiber obtained is then at least 1000 in an inert atmosphere.
By heating to (.degree. C.) and then to about 2500.degree. C. or above, the (112) cross lattice lines and (100) and (1
01) X-ray diffraction pattern characterized by the presence of lines, that is, having a three-dimensional structure of hardness, a layer spacing of 3.37Å or less, an apparent lamination dimension (La) of 100Å or more and 100 or more.
It has been reported that graphite fibers having an apparent stacking height (Lc) of 0 Å or more are produced (Japanese Patent Laid-Open No. 19197/1974).

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
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が優れてお
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 which is not necessarily optically anisotropic at the stage of spinning raw material pitch but has excellent spinnability, and which is optically anisotropic during the spinning or firing step, and A method for producing carbon fiber using the same has 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57-100186)が報告さ
れている。しかし、いずれの場合も水添処理が必要とさ
れている。また前者の場合は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, it does not substantially form mesophases, forms a homogeneous and optically isotropic single phase, and exhibits an orientation in that direction when an external force is applied. ~
A latent anisotropic pitch of 1.2 (JP-A-57-100186) has been reported. However, in any case, hydrogenation treatment is required. In the former case, there is no example of carbon fiber production by using only the primomethaze pitch, that is, the quinoline-soluble pitch, and the spinning pitch contains quinoline-insoluble matter.

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 a high elastic modulus has a fibrous structure and 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PAN
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的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。
All of the Pitch-based carbon fibers produced by the above method are PAN
Although it has superior graphitization characteristics compared to PF-based carbon fibers, it is still inferior in tensile strength as a fiber, and it is necessary to provide Pitch-based carbon fibers with mechanical properties equivalent to PAN-based carbon fibers. The reality is that it has not arrived.

本発明者らは、引張強さ、引張弾性率及破断伸びなどの
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,不融化及び焼成処理
するとにより得られるピツチ系炭素繊維は、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
造が賦与されておりしかも従来のピツチ系高性能炭素繊
維では発現されていない、高強度、高伸度の機械的特性
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 present inventors have conducted diligent research in order to develop a Pitch-based carbon fiber which is equal to or superior to the PAN-based carbon fiber in mechanical properties such as tensile strength, tensile modulus and elongation at break. As a result, spinning was performed using naphthalene as a raw material, heat-polymerized under specific conditions, and removing light components to obtain an optically isotropic pitch having a proper molecular structure and molecular weight as a spinning raw material pitch. Surprisingly, the Pitch-based carbon fiber obtained by infusibilizing and firing has a fiber structure in which the carbon net surface is selectively arranged in the fiber axis direction, and the conventional Pitch-based high-performance carbon fiber. Based on this finding, the present invention has been accomplished based on the finding that it has mechanical properties of high strength and high elongation, which are not expressed in.

すなわち、本発明は、X線回折により求めた配向角(2Z
゜)が50°より大きく、微結晶の見掛けの大きさ(L
c(002))が15〜50Åであり、層間隔(d002)が3.43〜
3.47Åを示すナフタリンを原料として900〜1600
℃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、900〜1600℃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, according to the present invention, the orientation angle (2Z
Is greater than 50 ° and the apparent size of the microcrystals (L
c (002) ) is 15 to 50Å, and the layer spacing (d 002 ) is 3.43 to
900-1600 using naphthalene showing 3.47Å as raw material
The object is to provide a Pitch-based carbon fiber treated at ° C. Another object of the present invention is to subject naphthalene to heat polymerization in the presence of a Lewis acid catalyst at 330 ° C. or lower for 0.5 to 100 hours to remove the catalyst, and then 330 to 440 while flowing an inert gas under normal pressure or reduced pressure. Heat to ℃ to remove light components, softening point is 180 ~ 200 ℃, H / C is 0.6
-0.8, the average molecular weight is 800-1500, the benzene-insoluble matter is 35-45% by weight, and an optically isotropic carbonaceous pitch containing no quinoline-insoluble matter is produced. According to the present invention, there is provided a method for producing a Pitch-based carbon fiber having the above-mentioned characteristics by performing spinning, infusibilization and carbonization and firing, and then treating at a temperature of 900 to 1600 ° C. under an inert 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50°より大きく、好ましくは50〜80°で
あり、微結晶の見掛けの大きさ(Lc(002))が15〜50
Åで、好ましくは20〜30Åであり、層間隔(d002)が
3.44〜3.47Å、好ましくは3.441〜3.461Åである。
The carbon fiber of the present invention has an orientation angle determined by X-ray diffraction.
(2Z °) is larger than 50 °, preferably 50 to 80 °, and the apparent size of fine crystals (L c (002) ) is 15 to 50.
Å, preferably 20 to 30Å, and the layer spacing (d 002 ) is
It is 3.44 to 3.47Å, preferably 3.441 to 3.461Å.

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、且つ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 to the conventional Pitch-based carbon fiber in mechanical properties. It shows the physical strength.

本発明の炭素繊維は、少なくとも200kgf/mm2の引張強さ
と、少なくとも9500kgf/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 200 kgf / mm 2, at least a tensile modulus of 9500kgf / 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
ことがなく、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, during infusibilization, the infusibilization reaction proceeds in the surface layer portion, whereby a fine mosaic structure is formed, In the central part, the infusible reaction does not disturb the preferred arrangement of the molecules and imparts an excellent fiber structure.

次に、本発明の製造方法について説明をする。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。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5〜5
0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
で好ましくない。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。
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. Examples of the Lewis acid catalyst used here include AlCl 3 and BF 3, but AlCl 3 is preferable.
The Lewis acid catalyst is 5 to 5 with respect to 100 parts by weight of naphthalene.
Although 0 parts by weight can be used, 8 to 20 parts by weight is preferable. still,
When the heating temperature is higher than 330 ° C., mesophase pitch is generated, and quinoline insoluble matter is 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, an average molecular weight of 800 to 1500, and a benzene insoluble content of 35 to 35.
It is 45% by weight, contains no quinoline-insoluble matter, and exhibits 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℃/分の昇温温度
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 to be 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. The infusibilizing treatment is performed by heating to 230 to 300 ° C. at a temperature rising temperature of 0.5 to 5 ° C./min in an oxidizing gas atmosphere and maintaining the temperature 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N2ガス中で900〜1600℃
の所定の温度で処理するかあるいは連続して900〜1
600℃の所定の温度で炭化焼成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 infusibilized fiber 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 ℃, then 900 to 1600 ℃ in N 2 gas
At a prescribed temperature of 900-1 or continuously
Carbon fiber can be obtained with a high carbonization yield by carbonizing and firing at a predetermined temperature of 600 ° C.

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(Lc)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) Structural related factors Orientation angle (2Z °), apparent size of crystallite in C-axis direction (L c ).
And the layer spacing (d 002 ) are structurally related factors that represent the higher order structure of the fiber determined from the wide-angle X-ray diffraction pattern. Orientation angle (2Z
(°) indicates the degree of orientation of the microcrystals with respect to the fiber axis direction, and the smaller this angle is, the more the orientation is advanced. The apparent size of the crystallites (L c ) represents the apparent stacking height of the carbon crystallites, and the layer spacing (d 002 ) represents the interplanar spacing between the carbon network planes of the crystallites.

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 (L c ) of the microcrystals was 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 along the diffraction ring is measured and 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、蒸気圧オスモメーター(VPO)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 pitch characteristics a) Molecular weight Measured using a vapor pressure osmometer (VPO) with pyridine as the solvent. As VPO, (Corona Model 117 molecular weight measuring device) 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より次式に従つて
算出する。
b) H / C Calculated according to the following formula from elemental analysis measured according to 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、上部から10kgf/cm2の荷
重をかけ、昇温速度6℃/分で昇温しつつ、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 high flow tester (Shimadzu Corporation), put 1g of crushed crushed particles 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. Then, the temperature of the inflection point of the plasticization curve is set as the softening point while the temperature is raised at a temperature rising rate of 6 ° C./min.

d)溶剤不溶分 JIS-K-2425に準拠して測定した。d) Insoluble matter in solvent Measured in accordance with 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JI
S 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による。
(3) Physical properties of carbon fiber The fiber diameter, tensile strength, elongation and tensile modulus of carbon fiber are JI.
Measure according to S R-7601 "Carbon fiber test method". still,
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/cm2
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を空気雰囲下で、約1
℃/分の昇温速度で、265℃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 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
It was extruded through the above nozzle and spun at a N 2 gas pressure of. The winding speed at this time was about 700 m / min. The pitch fiber obtained as described above was added to about 1 in an 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 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、この雰囲
気中に約30分間保持し処理した。
The fiber thus infusibilized was heated to 900 ° C. at a temperature rising rate of about 5 ° C./min in an N 2 gas atmosphere and kept in this atmosphere for about 30 minutes for processing.

得られた炭素繊維(直径:8.5μm)のX線回折より求
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: 8.5 μm) determined by X-ray diffraction.

実施例2 実施例1で得られた900℃で処理された炭素繊維をN
2ガス雰囲気下で約50℃/分の昇温速度で1200℃
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 2 The carbon fiber treated at 900 ° C. obtained in Example 1 was N
1200 ° C at a heating rate of about 50 ° C / min in a 2 gas atmosphere
It was heated up to and held 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3表に示す。
Table 3 shows the physical properties and mechanical properties of the obtained carbon fiber (diameter: 8 μm) determined by X-ray diffraction.

実施例3 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0kgf
/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
ス流通下で加熱し軽質分を除去した。
Example 3 Naphthalene (Kanto Chemical Co., Inc. first-grade reagent) 1000
g and 100 g of AlCl 3 (Kanto Kagaku 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 kgf.
/ cm 2 G, raise the temperature to 300 ° C with stirring, and
Polymerization was carried out at 0 ° C. for 1 hour. After the 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、偏光顕微鏡下で
観察したところ光学的等方性であり、かつその特性は第
4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 4.

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
2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 put into a cylinder having a nozzle having a diameter of 0.3 mm, heated and melted at 275 ° C., 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 ° C in an air atmosphere.
The pitch fibers were heated to 250 ° C. at a heating rate of / min, and 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、この
雰囲気中に約30分間保持し処理した。
The fiber thus infusibilized was heated to 900 ° C. at a temperature rising rate of about 5 ° C./min in an N 2 gas atmosphere and kept in this atmosphere for about 30 minutes for processing.

得られた炭素繊維(直径:8μm)のX線回折より求め
た物性及び機械的特性を第5表に示す。
Table 5 shows the physical properties and mechanical properties of the obtained carbon fiber (diameter: 8 μm) determined by X-ray diffraction.

実施例4 実施例3で得られた900℃で処理された炭素繊維をN
2ガス雰囲気下で約50℃/分の昇温速度で1200℃
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 4 The carbon fiber treated at 900 ° C. obtained in Example 3 was N
1200 ° C at a heating rate of about 50 ° C / min in a 2 gas atmosphere
It was heated up to and held 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6表に示す。
Table 6 shows the physical properties and mechanical properties of the obtained carbon fibers (diameter: 8 μm) determined by X-ray diffraction.

実施例5 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を攪拌機付き三口フラスコに仕込み、10
0℃,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、触媒除去のため水
洗、ロ過(孔径0.2μm)を行い、ピツチを得た。
Example 5 Naphthalene (Kanto Chemical Co., Inc. first-grade reagent) 1000
g and 100 g of AlCl 3 (first-class reagent manufactured by Kanto Chemical Co., Inc.) as a catalyst were charged in a three-necked flask equipped with a stirrer, and 10
Polymerization was carried out at 0 ° C. for 60 hours. Next, 100 g of AlCl 3 (first-class reagent manufactured by Kanto Chemical Co., Inc.) as a catalyst was further added, and 210
Polymerization was performed at 30 ° C. for 30 hours. After the completion of the polymerization, the catalyst was removed by washing with water and filtration (pore size: 0.2 μm) to obtain a pitch.

得られたピツチを380℃、10Torr、20分間N2
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 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7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 7.

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
2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 extruded and 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.

上述のようにして得られたピツチ繊維を空気雰囲下で約
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 fiber obtained as described above was heated to 265 ° C. at a temperature rising rate of about 1 ° C./min in an air atmosphere, and the pitch fiber was 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、この
雰囲気に約30分間保持し、処理した。
The fiber thus infusibilized was heated to 900 ° C. at a temperature rising rate of about 5 ° C./min in an N 2 gas atmosphere and kept in this atmosphere for about 30 minutes to be treated.

得られた炭素繊維(直径:8μm)のX線回折より求め
た物性及び機械的特性を第8表に示す 実施例6 実施例5で得られた900℃で処理された炭素繊維をN
2ガス雰囲気下で約50℃/分の昇温速度で1200℃
まで加熱して、この雰囲気下で約10分間保持し処理し
た。
Table 8 shows the physical properties and mechanical properties of the obtained carbon fiber (diameter: 8 μm) determined by X-ray diffraction. Example 6 The carbon fiber treated at 900 ° C. obtained in Example 5 was N
1200 ° C at a heating rate of about 50 ° C / min in a 2 gas atmosphere
It was heated up to and held 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9表に示す。
Table 9 shows the physical properties and mechanical properties of the obtained carbon fiber (diameter: 8 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5
0°より大きく、微結晶の見掛けの大きさ(Lc(002)
が15−50オングストロームであり、層間隔
(d002)が3.44−3.47オングストロームを示
す、900℃−1600℃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 5
Greater than 0 ° and apparent size of microcrystal (L c (002) )
Is 15-50 angstroms and the layer spacing (d 002 ) is 3.44-3.47 angstroms, and the carbon fiber made from naphthalene as a raw material treated at a temperature of 900 ° C-1600 ° C.
【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、
不融化した後、900−1600℃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50°より大きく、微結晶の見掛けの大きさ(L
c(002))が15−50オングストロームであり、層間隔
(d002)が3.44−3.47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,
Orientation angle (2Z °) determined by X-ray diffraction, characterized by being treated at a temperature of 900-1600 ° C after infusibilization
Is larger than 50 ° and the apparent size of the microcrystal (L
c (002)) is 15-50 Angstroms method of producing a carbon fiber layer spacing (d 002) indicates 3.44-3.47 Å.
JP59193245A 1984-09-14 1984-09-14 Carbon fiber and manufacturing method thereof Expired - Lifetime JPH0633528B2 (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
JP59193245A JPH0633528B2 (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
FR8513616A FR2570395B1 (en) 1984-09-14 1985-09-13 PROCESS FOR THE PREPARATION OF CARBON FIBERS AND CARBON FIBERS PRODUCED BY THIS PROCESS
DE3546613A DE3546613C2 (en) 1984-09-14 1985-09-13
DE19853532785 DE3532785A1 (en) 1984-09-14 1985-09-13 METHOD FOR PRODUCING CARBON FIBERS AND CARBON FIBERS PRODUCED BY THIS METHOD
GB08522741A GB2164351B (en) 1984-09-14 1985-09-13 Process for producing carbon fibers and pitch suitable for use therein
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
JP59193245A JPH0633528B2 (en) 1984-09-14 1984-09-14 Carbon fiber and manufacturing method thereof

Publications (2)

Publication Number Publication Date
JPS6183317A JPS6183317A (en) 1986-04-26
JPH0633528B2 true JPH0633528B2 (en) 1994-05-02

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Country Link
JP (1) JPH0633528B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2648711B2 (en) * 1986-11-07 1997-09-03 株式会社 ペトカ Manufacturing method of pitch-based carbon fiber three-dimensional fabric
JPS63303124A (en) * 1987-01-28 1988-12-09 Petoka:Kk Pitch-based carbon fiber and production thereof

Family Cites Families (6)

* 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
JPS5663012A (en) * 1979-10-24 1981-05-29 Mitsubishi Rayon Co Ltd Preparation of carbon fiber having high performance
JPS5818421A (en) * 1981-07-27 1983-02-03 Agency Of Ind Science & Technol Preparation of carbon fiber
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
JPS5936726A (en) * 1982-08-24 1984-02-29 Agency Of Ind Science & Technol Precursor pitch fiber for carbon fiber

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