JPS58142975A - Mesophase pitch and preparation of carbon fiber using it - Google Patents

Mesophase pitch and preparation of carbon fiber using it

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Publication number
JPS58142975A
JPS58142975A JP2490082A JP2490082A JPS58142975A JP S58142975 A JPS58142975 A JP S58142975A JP 2490082 A JP2490082 A JP 2490082A JP 2490082 A JP2490082 A JP 2490082A JP S58142975 A JPS58142975 A JP S58142975A
Authority
JP
Japan
Prior art keywords
pitch
mesophase
catalytic cracking
oil
fraction
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2490082A
Other languages
Japanese (ja)
Inventor
Haruo Shibatani
柴谷 治雄
Kunimasa Takahashi
高橋 邦昌
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 Petrochemical Co Ltd
Original Assignee
Mitsubishi Petrochemical Co Ltd
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 Petrochemical Co Ltd filed Critical Mitsubishi Petrochemical Co Ltd
Priority to JP2490082A priority Critical patent/JPS58142975A/en
Publication of JPS58142975A publication Critical patent/JPS58142975A/en
Pending legal-status Critical Current

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

Abstract

PURPOSE:To obtain carbon fibers having high strength and high modulus, by spinning mesophase pitch obtained by heating in an inert gas atmosphere at high temperature isotropic carbonaceous pitch prepared from an oil at a column bottom of the catalytic cracking product of petroleum fraction, making it infusible and carbonizing it. CONSTITUTION:Isotropic carbonaceous pitch obtained by distilling an oil at a column bottom (catalytic cracking bottom) formed by the catalytic cracking of a petroleum fraction (distilled oil of kerosine, etc., distillation residue, distillate prepared by subjecting crude oil or its fraction to hydrogenolysis, etc.) is heat- treated at 430-550 deg.C (preferably 450-510 deg.C) usually for 10sec-150min (preferably 2-100min) with introducing an intert gas (e.g., nitrogen etc.) in a rate of 200-5,000l/time/1kg raw material pitch into it, to give 40-100wt% mesophase (containing about 40wt% quinoline-soluble mesophase). This mesophase pitch is spun (at 300-450 deg.C at about 50-1,000m/min), made infusible (at 250-400 deg.C for about 5-60min) in an oxidative atmosphere, and carbonized (at 900-2,000 deg.C for about 0.5-30min), to give carbon fibers.

Description

【発明の詳細な説明】 本発明は、メソフェーズピッチおよびそれを利用して炭
素繊維を製造する方法に関するものであるO 本発明によれば、キノリン可溶性のメンフェーズを含む
メソフェーズピッチを、抽出等の特別の処理を施すこと
なく、短い熱処理時間で製造することができ、該メン7
エーズビツチから容易に炭素繊維を製造することができ
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to mesophase pitch and a method for producing carbon fiber using the same.According to the present invention, mesophase pitch containing quinoline-soluble menphase is extracted by It can be manufactured in a short heat treatment time without any special treatment, and the
Carbon fiber can be easily produced from Azubitsu.

市販の炭素繊維の大部分は、現在ポリアクリロニトリル
繊維から造られている。しかし、これらは原料のポリア
クリロニトリル繊維が高価なこと、得られる炭素繊維の
収率が低いこと等のためにきわめて高価である。これに
対して炭素質ピッチを原料とする方法は、原料が安価で
炭素繊維の収率が高いため、安価な炭素繊維の製法とし
て近年特に関心を集めている。
The majority of commercially available carbon fibers are currently made from polyacrylonitrile fibers. However, these are extremely expensive because the raw material polyacrylonitrile fiber is expensive and the yield of carbon fiber obtained is low. On the other hand, a method using carbonaceous pitch as a raw material has attracted particular attention in recent years as a method for producing inexpensive carbon fibers because the raw material is inexpensive and the yield of carbon fibers is high.

光学的に等方性のピッチから得られる炭嵩繊維は、強電
−弾性率ともに小さい。高強賓高弾性率の線素繊維を得
るために#j1等方性ピッチに熱処理を加え、一種の液
晶であるメソフェーズを形成させる必要がある。このよ
うなメソフェーズを含77エーズビツチと呼ぶ。代表的
なメソ7エーズビツチの製法は、たとえば特公昭54−
1810号公報に記載されているように、等方性ピッチ
を400℃で17時間加熱するものであり、これによっ
て約50幇のメソフェーズが形成される。しかし、この
方法で得られたメソフェーズは、#1はすべてがキノリ
ンあるいはピリジンに不溶であ抄、このためメソフェー
ズピッチの軟化点が高く、紡糸が困難になる問題点があ
った。
Carbon bulk fibers obtained from optically isotropic pitch have low ferroelectric modulus and low elastic modulus. In order to obtain a linear fiber with high strength and high elastic modulus, it is necessary to heat-treat the #j1 isotropic pitch to form a mesophase, which is a type of liquid crystal. Such a mesophase is called a mesophase. The typical manufacturing method for meso 7A's bitch is, for example,
As described in Japanese Patent No. 1810, isotropic pitch is heated at 400° C. for 17 hours, thereby forming a mesophase of about 50 degrees. However, the mesophase #1 obtained by this method is entirely insoluble in quinoline or pyridine and is therefore difficult to spin due to the high softening point of the mesophase pitch.

とれに対して、キノリン可溶性のメン7エーズを含むメ
ツフェーズピッチは、軟化点が低いため紡糸が容易にな
る利点があり、近年高性能炭素線ツイテの研究が積極的
に行なわれている。キノリン可溶性のメソフェーズを含
むメソ7エーズピツチの製造法に関する先行技術に#i
次の様なものがある。
In contrast, metsuphase pitch, which contains quinoline-soluble men-7Aze, has the advantage of being easier to spin due to its lower softening point, and research into high-performance carbon wire threads has been actively conducted in recent years. #i in the prior art regarding the production method of meso-7Aze pitch containing quinoline-soluble mesophase
There are the following.

%開昭54−160427号公報では、等力性ピッチを
溶媒で抽出し、その不溶分子230〜400℃に加熱す
ることによって、キノリン可溶性のメソフェーズを得て
いる。この発明者は、これをネオメソフェーズ、加熱前
の溶剤不溶分をネオメソフェーズ生成画分(NMF画分
)と呼んでいる。
In Japanese Patent Publication No. 54-160427, a quinoline-soluble mesophase is obtained by extracting isotropic pitch with a solvent and heating the insoluble molecules at 230 to 400°C. The inventor calls this neomesophase, and the solvent-insoluble fraction before heating is called the neomesophase-forming fraction (NMF fraction).

特開昭55−58287号公報では、ピッチを予め35
0〜480″’Cにおいて、メンフェーズ小球の生成直
前まで加熱することによって、NMF画分の量を増加さ
せている。
In Japanese Patent Application Laid-Open No. 55-58287, the pitch is set to 35 in advance.
The amount of NMF fraction is increased by heating at 0-480''C until just before the formation of menphase globules.

特開昭55−130809号公報では、ピッチを脱アル
キル触媒で処理することによって、NMF画分を増加さ
せている。
In JP-A-55-130809, the NMF fraction is increased by treating pitch with a dealkylation catalyst.

特開昭55−144087号公報では、ピップを加熱処
理したのち、有機溶媒を加えて懸濁する不溶分を除き、
さらに反溶媒を加えてNMF画分を沈澱分離している。
In JP-A-55-144087, after heat-treating pip, an organic solvent is added to remove suspended insoluble matter,
Further, an antisolvent is added to separate the NMF fraction by precipitation.

特開昭56−2388号公報では、ピッチを250〜3
80℃で減圧処理したのち350〜450℃で大気圧下
熱処理、を九Ifi350〜450℃で減圧下熱処理す
ることによってピッチ中の芳香族油分を除去し、引き続
き溶媒で抽出することによってNMF画分を得ている。
In Japanese Patent Application Laid-Open No. 56-2388, the pitch is set to 250 to 3.
After vacuum treatment at 80°C, heat treatment at 350-450°C under atmospheric pressure to remove the aromatic oil in the pitch, followed by extraction with a solvent to obtain the NMF fraction. I am getting .

特開昭56−109807号公報では、ピッチに有機溶
媒を加えて350〜450℃に加熱し、不溶分を除いた
のち反溶媒を加えてNMFlij分を得ている。
In JP-A-56-109807, an organic solvent is added to pitch, heated to 350 to 450°C, insoluble matter is removed, and an antisolvent is added to obtain NMFlij.

特開昭56−167788号公報では、沸点200〜5
50℃の接触分解ボトムよ抄沸点400℃以下の留分を
除いた後、390〜450℃で熱処理し、引き続き減圧
下320〜380℃で油分を除き、更に有機溶媒を加え
て不溶分を除去し、反溶媒を加えてNMFllii分を
得ている。
In JP-A-56-167788, the boiling point is 200-5.
After removing the fraction with a boiling point of 400°C or less from the catalytic cracking bottom at 50°C, heat treatment is performed at 390 to 450°C, followed by removing oil at 320 to 380°C under reduced pressure, and further adding an organic solvent to remove insoluble matter. Then, an anti-solvent was added to obtain the NMFllii fraction.

特開昭57−2393号公報では、反溶媒を複数段で加
えることによって、軟化点の異るNMF画分を得ている
In JP-A-57-2393, NMF fractions with different softening points are obtained by adding an antisolvent in multiple stages.

特開昭54−55625号公報では、等方性ピッチを3
80〜430℃で攪拌しながら不活性ガスを通じて熱処
理し、ピリジン可溶性のメソフェーズを含むメンフェー
ズピッチを得ている。この方法の加熱時間は、2〜60
時間である。
In Japanese Patent Application Laid-open No. 54-55625, the isotropic pitch is set to 3.
A heat treatment is performed at 80 to 430° C. with stirring while passing an inert gas through the mixture to obtain menphasic pitch containing pyridine-soluble mesophase. The heating time for this method is 2 to 60
It's time.

特開昭56−57881号公報では、ピッチに溶剤抽出
などの物理的操作を加えることKよって、ピリジン可溶
性のメソフェーズを含むメソフェーズピッチを得ている
In JP-A-56-57881, mesophase pitch containing pyridine-soluble mesophase is obtained by subjecting pitch to physical operations such as solvent extraction.

特開昭56−101915号公報では、エチレンタール
などのピッチ前駆物質を400〜550℃で加圧熱処理
した徒、不活性ガスを通じて大気圧下に熱処理するとと
によって、ピリジン6エ溶性メンフエーズ含有メンフエ
ーズピツチを得でいる。
In JP-A-56-101915, pitch precursors such as ethylene tar are heat-treated under pressure at 400 to 550°C, and then heat-treated under atmospheric pressure through an inert gas to produce a membrane containing pyridine 6-ethyl soluble memphase. I'm getting ace pitch.

これらの公知技術の他に、ピッチをテトラハイドロキノ
リンと約400℃で反応させたのち、約500℃で減圧
下に短時間熱処理することによってプリメンフェーズと
呼ぶ等方性ピッチを得、これより高性能の炭素繊維を得
る方法が発表されている(昭和56年8月22日付日本
経済新聞)。
In addition to these known techniques, pitch is reacted with tetrahydroquinoline at about 400°C and then heat-treated at about 500°C for a short time under reduced pressure to obtain an isotropic pitch called premenphase. A method for obtaining high-performance carbon fiber has been announced (Nihon Keizai Shimbun, August 22, 1981).

上述した様に、公知技術は、メソフェーズピッチを製造
するのに抽出等の特別の処理が必要、工程が複雑、処理
時間が長い等の問題があった。
As described above, the known techniques have problems such as the need for special processing such as extraction to produce mesophase pitch, complicated processes, and long processing times.

本発明者らは、上記公知技術に比較し、商業的rc製造
する場合に有利な石油留分の接触分解で生成する塔底油
からのメソフェーズピッチ及びそれを利用して炭素繊維
を製造する方法について、種々の処理条件を検討した結
果、これまで通常用いられなかった高温度領絨で、減圧
下に処理を行うと、特別の処理を施すことなく、キノリ
ン町溶性のメンフェーズを含む低軟化点のメソフェーズ
ピッ革が得られ、該ピッチはそのまま容易に紡糸されて
高性能の炭素繊維となることを見い出し本発明を完成し
た。
The present inventors have discovered mesophase pitch from tower bottom oil produced by catalytic cracking of petroleum fractions, which is advantageous in commercial RC production, and a method for producing carbon fiber using the same, compared to the above-mentioned known technology. As a result of examining various processing conditions, we found that if the treatment is carried out under reduced pressure in a high-temperature chamber that has not been normally used, a low-softening agent containing quinoline-soluble menphase can be obtained without special treatment. It was discovered that a mesophase pitch leather of dots was obtained, and that the pitch could be easily spun as it was to form high-performance carbon fiber, and the present invention was completed.

部ち、本発明の第1#′i、石油声分の接触分解で生成
する塔底油から得られる等方性の炭素質ピッが生成する
まで加熱して得られるメソフェーズピッチを、第2は、
石油留分の接触分解で生成する塔底油から得られる等方
性の炭素質ピッチを、不するまで加熱して得られるメン
フェーズピッチを、紡糸、不融化および炭化することを
特徴とする炭素繊維の製造方法を提供するものである。
In the first part #'i of the present invention, the mesophase pitch obtained by heating until an isotropic carbonaceous pitch obtained from the bottom oil produced by catalytic cracking of petroleum fraction is produced, in the second part. ,
Carbon characterized by spinning, infusible, and carbonizing isotropic carbonaceous pitch obtained from tower bottom oil produced by catalytic cracking of petroleum fractions, and menphasic pitch obtained by heating until solidification. A method for producing fibers is provided.

本発明のメンフェーズピッチは、炭素繊維の他、フィル
ム、シート等の炭素成型品の製造VC用いることができ
、一方、該炭素繊維は、高性能補強祠、充填剤等に利用
される。
The menphase pitch of the present invention can be used in the production of carbon molded products such as films and sheets in addition to carbon fibers, and on the other hand, the carbon fibers can be used in high-performance reinforcing stones, fillers, and the like.

本発明に使用される原料ピッチは、石油留分の接触分解
で生成する塔底油C接触分解ボトム)が用いられる。こ
こで石油留分とは、灯油・軽油等の留出油、蒸留残渣、
原油、およびこれらの留分に水素化分解、水添脱硫等の
処理t−紬して生成する留分尋をいう。九とえば、接触
分解ボトムから蒸留によ抄常圧換算沸点450℃以下の
留分を除いえピッチ等が用いられる。また、上記の塔底
油に適当な処理を加えて得られる石油ピッチも用いられ
る。市販の石油ピッチ、例えば、アシュランド240(
アシュランド拳オイル社製)などを用いることもできる
The raw material pitch used in the present invention is column bottom oil C (catalytic cracking bottoms) produced by catalytic cracking of petroleum fractions. Petroleum fractions here refer to distillate oils such as kerosene and light oil, distillation residues,
It refers to crude oil and the fractions produced by subjecting these fractions to treatments such as hydrocracking and hydrodesulfurization. For example, pitch or the like is used, which is obtained by removing the fraction having a boiling point of 450°C or less in terms of normal pressure from the catalytic cracking bottoms by distillation. Petroleum pitch obtained by appropriately treating the above-mentioned tower bottom oil may also be used. Commercially available petroleum pitches, such as Ashland 240 (
(manufactured by Ashland Fist Oil Co.) etc. can also be used.

本発明に用いられる熱処理の温度範囲は、430〜55
0℃、好ましくは440〜530℃であり、殊に450
〜510℃が好ましい。熱処理の温度[,550℃を越
えて用いることもできるが、極めて短い時間でメソフェ
ーズピッチが生成し、この温度で熱処理が長くなると該
メンフェーズピッチのキノリン可溶性部分が急速に減少
するので、これを利用する炭素繊維製造が困難になるな
ど好ましいものではない。逆に、熱処理温度が430℃
未満では、メソフェーズの生成に長時間を賛し好ま【、
<ない。
The temperature range of the heat treatment used in the present invention is 430 to 55
0°C, preferably 440-530°C, especially 450°C
~510°C is preferred. Although it is possible to use a heat treatment temperature exceeding 550°C, mesophase pitch is formed in an extremely short period of time, and if the heat treatment is prolonged at this temperature, the quinoline-soluble portion of the mesophase pitch will rapidly decrease. This is not desirable as it makes it difficult to manufacture the carbon fibers used. On the contrary, the heat treatment temperature is 430℃
It is preferable to take a long time to generate the mesophase.
<No.

熱処理に要する時間は、原料ピッチ、熱処理温度等によ
って異るが、通常10秒〜150分、好ましく#′i1
〜120分、殊に好ましくtj2〜!00分が用いられ
る。
The time required for heat treatment varies depending on the raw material pitch, heat treatment temperature, etc., but is usually 10 seconds to 150 minutes, preferably #'i1
~120 minutes, particularly preferably tj2~! 00 minutes is used.

本発明は、上記熱処理を行う場合、不活性ガスを吹込み
ながら行う。該不活性ガスとしては、窒素、アルゴンの
他に水素、メタン、エタン等の室温でガス状の炭化水素
及び少なくとも熱処理温度でガス状となる炭化水素、ス
チーム等が用いられる。吹込み量は、原料ピッチlb当
り200〜5.000 t7時間、好ましくは400〜
3,000t/時間である。
In the present invention, when performing the above heat treatment, it is performed while blowing an inert gas. As the inert gas, in addition to nitrogen and argon, hydrogen, methane, ethane, and other hydrocarbons that are gaseous at room temperature, hydrocarbons that are gaseous at least at the heat treatment temperature, steam, and the like are used. The amount of injection is 200 to 5,000 t per lb of raw material pitch for 7 hours, preferably 400 to 5,000 t per lb of raw material pitch.
3,000t/hour.

本発明の高性能のメソフェーズピッチが得られるその生
成機構は明らかではない。しかし、不活性ガスを吹込み
ながら、特定の熱処理温度で加熱する必要があり、どち
らか一方の条件を満足するだけの方法では、高性能のメ
ンフェーズピッチは製造できない。
The mechanism by which the high-performance mesophase pitch of the present invention is obtained is not clear. However, it is necessary to heat at a specific heat treatment temperature while blowing inert gas, and high-performance menphase pitch cannot be produced by a method that only satisfies one of the conditions.

本発明は、原料ピッチを攪拌しながら行うことが好まし
いが必須ではない。
The present invention is preferably carried out while stirring the raw material pitch, but it is not essential.

さらに、本発明は、上記不活性ガスを吹込みながら熱処
理を行うものであるが、熱処理を行いながら不活性ガス
の吹込みのみを中断!−1系を減圧にして熱処理を続行
することもできる。
Furthermore, in the present invention, the heat treatment is performed while blowing in the inert gas, but only the blowing of the inert gas is interrupted while the heat treatment is being performed! The heat treatment can also be continued by reducing the pressure in the -1 system.

ソフエーズビツチに含有される該メン7エーズの約60
4X以下であり、該メンフェーズに対して約40%以上
のキノリン可溶性メンフェーズを含むものである。
Approximately 60% of the Men 7 Aes contained in Sofa's Bitch
4X or less, and contains about 40% or more of quinoline-soluble menphase relative to the menphase.

ここで、メソフェーズの含有率は室温におけるめる比率
を示すものである。
Here, the content of mesophase indicates the mesophase ratio at room temperature.

また、本発明のメソフェーズピッチは、軟化点が通常3
00℃以下であり、容易に紡糸し得る本の、である。
Furthermore, the mesophase pitch of the present invention usually has a softening point of 3.
00°C or less and can be easily spun.

本発明のメンフェーズピッチは、公知の溶融紡糸法によ
って紡糸することが・できる。紡糸温暖は、ピッチの帖
1特姓等に依存するが例えば300〜400℃が用いら
れる。紡糸速度は、200〜1000m/分、又はこれ
以上の高速でも紡糸でこれによって約5〜約15μmの
ピッチ繊維が得られる。ピッチ繊維は引き続き酸素含有
ガス等の酸化性雰囲気下において、例えは250〜40
0℃、約5〜約60分間不融化処理され、更に、窒素、
アルゴン等の不活性ガス雰囲気下例えば、900〜20
00℃で、約0.5〜約30分で炭化処理される。所望
ならば、更に前記不活性ガス雰囲気下2500〜330
0℃で処理し、黒鉛繊維とすることもできる。また、上
記の各処理において、公知の改良方法(例えば、特開昭
55−6547号、同56−101916号各公報等に
開示の方法)を適用することも可能である。
The menphase pitch of the present invention can be spun by a known melt spinning method. Although the spinning temperature depends on the characteristics of the pitch, for example, 300 to 400°C is used. The spinning speed may be 200 to 1000 m/min or even higher, thereby obtaining pitch fibers of about 5 to about 15 μm. The pitch fiber is then heated under an oxidizing atmosphere such as an oxygen-containing gas, for example, at a temperature of 250 to 40
Infusibility treatment was performed at 0°C for about 5 to about 60 minutes, and nitrogen,
Under an inert gas atmosphere such as argon, for example, 900 to 20
Carbonization treatment is carried out at 00°C for about 0.5 to about 30 minutes. If desired, further under the inert gas atmosphere 2500 to 330
Graphite fibers can also be obtained by processing at 0°C. Further, in each of the above-mentioned processes, it is also possible to apply a known improvement method (for example, the method disclosed in Japanese Patent Laid-Open Nos. 55-6547 and 56-101916, etc.).

以下に実施例を挙げて、本発明を更に具体的に説明する
The present invention will be explained in more detail with reference to Examples below.

実施例1 接触分解ボトムから、蒸留によって常圧換算沸点480
℃以下の留分を除去して、等方性ピッチを得た。このピ
ッチは、数平均分子量373、加熱ステージ付顕微鏡観
察による軟化点85℃、元素分析値はC:91.7%、
H: 5.9%、N : 0.2%、S:1.5%であ
った。
Example 1 From the catalytic cracking bottom, the boiling point in terms of normal pressure is 480 by distillation.
The fraction below ℃ was removed to obtain isotropic pitch. This pitch has a number average molecular weight of 373, a softening point of 85°C when observed under a microscope with a heating stage, and an elemental analysis value of C: 91.7%.
H: 5.9%, N: 0.2%, S: 1.5%.

このピッチ10fを内容積40−の反応器に入れ、アル
ゴン気渡下で、予め490℃に保った溶融塩浴に浸漬し
た。浸漬4分後、該ピッチが約485℃に達し九ので、
アルゴンを24t/時間で吹込みながら、その温暖で1
7分熱処理を行なった。その結果、生成した熱処理ピッ
チの収率は原料ピッチに対して33重量%、軟化点は2
70℃、メンフェーズ含有率1j85%、JIS  K
2425遠心法によるキノリンネ溶分tj44%であっ
た。
This pitch 10f was placed in a reactor having an internal volume of 40 -, and immersed in a molten salt bath previously maintained at 490° C. under an argon atmosphere. After 4 minutes of soaking, the pitch reached about 485°C, so
1 at that warm temperature while blowing argon at 24 tons/hour.
Heat treatment was performed for 7 minutes. As a result, the yield of the heat-treated pitch produced was 33% by weight based on the raw material pitch, and the softening point was 2.
70℃, Menphase content 1j85%, JIS K
The quinorine soluble fraction tj determined by the 2425 centrifugation method was 44%.

実施例2 実施例1で得られた熱処理ピッチt400℃において、
孔直径0.5■の紡糸口金を用いて420m/分で溶融
紡糸した。引き続き、空気雰囲気中tcて3.5時間で
270℃まて昇温し、そのi1電に45分保って不融化
した。さらにアルゴン気流中5℃/分で1000℃まで
加熱して炭素繊維を得た。得られた繊維は直径12μm
で、偏光顕微鏡観察において軸方向に配向した異方性を
示した。
Example 2 At the heat treatment pitch t400°C obtained in Example 1,
Melt spinning was carried out at 420 m/min using a spinneret with a hole diameter of 0.5 .mu.m. Subsequently, the temperature was raised to 270° C. over 3.5 hours in an air atmosphere, and the temperature was maintained at that temperature for 45 minutes to make it infusible. Further, carbon fibers were obtained by heating to 1000° C. at 5° C./min in an argon stream. The obtained fiber has a diameter of 12 μm
It showed anisotropy oriented in the axial direction when observed under a polarizing microscope.

また、引張り強tti186[1t/■冨、弾性率は1
1000麺/■意であった。
In addition, the tensile strength is 186 [1 t/■, the modulus of elasticity is 1
It was 1000 noodles/■.

上記実株例から、本発明の方法でメソフェーズピッチが
得られ、これを利用して高性能炭素繊維が製造できるこ
とが明らかである。
From the above actual examples, it is clear that mesophase pitch can be obtained by the method of the present invention and that high-performance carbon fiber can be manufactured using this.

以   上 特許出願人  三菱油化株式会社 代理人 弁理士 古 川 秀 利 代理人 弁理士 長 谷 正 久 手続補正書(自発) 昭和57年5月14旧 %1■島田春樹殿 1、 事件の表示  昭和57年特許願第24900号
2、 発明の名称  メソフェーズピッチおよびそれを
利用して炭素繊維を製造する方法 3 補正をする名 事件との関係  特許出願人 住所 東京都千代田区丸の内二丁目5番2号氏名 (6
05)  三菱油化株式会社4、代理人 住所 東京都千代田区丸の内二丁目5番2号5 補正の
対象 明細書の発明の詳細な説明の欄 i 補正の内容 (1)  第11頁第2〜12行の記載を削除し、次の
文章を挿入する。
Patent applicant Mitsubishi Yuka Co., Ltd. Agent Hidetoshi Furukawa Patent attorney Masahisa Hase Procedural amendment (voluntary) May 14, 1981 Old % 1 Haruki Shimada 1, Indication of the case 1982 Patent Application No. 24900 2 Title of the invention Mesophase pitch and method for producing carbon fiber using the same 3 Relationship to famous case for amendment Patent applicant address 2-5-2 Marunouchi, Chiyoda-ku, Tokyo Name (6)
05) Mitsubishi Yuka Co., Ltd. 4, Agent address: 2-5-2-5 Marunouchi, Chiyoda-ku, Tokyo Detailed description of the invention in the specification subject to amendment i Contents of amendment (1) Page 11, No. 2-5 Delete the 12th line and insert the following sentence.

[本発明の方法によって得られるメソフェースヒツチ中
には、メソフェーズが40〜100シ、好ましくは60
〜100%、より好ましくは70〜100シ含まれる。
[The mesophase hit obtained by the method of the present invention contains 40 to 100 mesophases, preferably 600 mesophases.
~100%, more preferably 70-100%.

殊に該含蓄が40%より少ない場合には該ピッチから得
られる炭素繊維の性能が低くなる・ここで、該メンフェ
ーズの含有率は室温における一光一微鏡観察によって求
めたもので、試料である該メソフェーズピッチの偏光m
徽m視對(等方性部分及び異方性部分を含む)中の異方
性部分の占める面積の全体に対する比率をボすものであ
る。また、上記メソフェーズピッチ中のキノリンネ溶分
は60%以下、好ましくは50%以下、よ抄好ましく 
Fi40%以−トである。キノリンネ溶分の比率が大き
い4134鶴ピツチの紡糸性が愚くなる。」 (2)  第x1!末第3〜2行に「300〜400℃
」とあるのを「300〜450℃」と訂正する。
In particular, if the content is less than 40%, the performance of the carbon fiber obtained from the pitch will be poor.Here, the menphase content was determined by one-light, one-microscope observation at room temperature, and Polarization m of a certain mesophase pitch
This indicates the ratio of the area occupied by the anisotropic portion in the view (including the isotropic portion and the anisotropic portion) to the total area. Further, the quinolinole dissolved content in the mesophase pitch is 60% or less, preferably 50% or less, preferably Yosho.
Fi is 40% or more. The spinnability of 4134 Tsuru Pituchi, which has a large proportion of quinoline dissolved matter, becomes poor. ” (2) No. x1! In the 3rd to 2nd lines at the end of the page, “300 to 400℃
'' should be corrected to ``300-450℃.''

(37@11真木第2〜1行に[200〜1000m/
分]とあるのを[50〜1000m/分]と訂正する。
(37 @ 11 Maki 2nd to 1st row [200 to 1000m/
[minute] should be corrected to [50-1000m/minute].

(4)第14頁第6行の後に以下の実施例3〜8を追加
する。
(4) Add the following Examples 3 to 8 after page 14, line 6.

[一実施例3〜5 熱処理条件を表−1とした他は実施例1と同様にして熱
処理ピッチを4#良。但し、溶融塩浴ii!度は反応温
度よ抄約5℃高くした。得られた結果線表−1に示した
通りであつ九。
[Examples 3 to 5 The heat treatment pitch was 4# Good in the same manner as in Example 1 except that the heat treatment conditions were as shown in Table 1. However, molten salt bath II! The temperature was about 5°C higher than the reaction temperature. The obtained results are as shown in Table 1.

(以下余白) 実施例6〜8 夷り列3〜5で得た熱処理ピッチを、孔直径0.5mの
紡糸口金を用いて溶融紡糸した。
(The following is a blank space) Examples 6 to 8 The heat-treated pitches obtained in rows 3 to 5 were melt-spun using a spinneret with a hole diameter of 0.5 m.

紡糸温度及び紡糸速度は表−2に示した通りであった。The spinning temperature and spinning speed were as shown in Table-2.

表−2 」 以上Table-2 ” that's all

Claims (4)

【特許請求の範囲】[Claims] (1)  石油留分の接触分解で生成する塔底油から得
られる等方性の炭素質ヒツチを、不活性ガスまで加熱し
て得られるメソフェーズピッチ。
(1) Mesophase pitch obtained by heating isotropic carbonaceous gas obtained from column bottom oil produced by catalytic cracking of petroleum fractions to an inert gas.
(2)  キノリン可溶性メソフェーズが、メソフェー
スヒツチに含有されるメソフェーズの約40X以上であ
る特許請求の範囲第1項記載のメンフェーズピッチ。
(2) The menphase pitch according to claim 1, wherein the quinoline-soluble mesophase is about 40 times or more of the mesophase contained in the mesophase hit.
(3)石油留分の接触分解で生成する塔底油から得られ
る等方性の炭素質ピッチを、不活性ガスを吹込みながら
、430〜550℃の温廖範囲0 で、−〜100%のメソフェーズが生成するまで加熱し
て得られるメソ7エーズピツチを、紡糸、不融化および
炭化することt4I黴とする炭素繊維の製造方法。
(3) Isotropic carbonaceous pitch obtained from tower bottom oil produced by catalytic cracking of petroleum fractions is heated to -100% at a temperature range of 430 to 550°C, while blowing inert gas. A method for producing carbon fibers, in which meso7Aze pitch obtained by heating until mesophase is produced is spun, infusible, and carbonized to produce t4I mold.
(4)  キノリン可溶性メンフェーズが、メソフェー
スヒツチに含有されるメソフェーズの約40%以上であ
る特許請求の範囲第3項記載の方法。
(4) The method according to claim 3, wherein the quinoline-soluble menphase accounts for about 40% or more of the mesophase contained in the mesophase hit.
JP2490082A 1982-02-18 1982-02-18 Mesophase pitch and preparation of carbon fiber using it Pending JPS58142975A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2490082A JPS58142975A (en) 1982-02-18 1982-02-18 Mesophase pitch and preparation of carbon fiber using it

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2490082A JPS58142975A (en) 1982-02-18 1982-02-18 Mesophase pitch and preparation of carbon fiber using it

Publications (1)

Publication Number Publication Date
JPS58142975A true JPS58142975A (en) 1983-08-25

Family

ID=12151051

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2490082A Pending JPS58142975A (en) 1982-02-18 1982-02-18 Mesophase pitch and preparation of carbon fiber using it

Country Status (1)

Country Link
JP (1) JPS58142975A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6128020A (en) * 1984-07-17 1986-02-07 Osaka Gas Co Ltd Preparation of carbon fiber

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6128020A (en) * 1984-07-17 1986-02-07 Osaka Gas Co Ltd Preparation of carbon fiber

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