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JPS6154352B2 - - Google Patents
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JPS6154352B2 - - Google Patents

Info

Publication number
JPS6154352B2
JPS6154352B2 JP57015520A JP1552082A JPS6154352B2 JP S6154352 B2 JPS6154352 B2 JP S6154352B2 JP 57015520 A JP57015520 A JP 57015520A JP 1552082 A JP1552082 A JP 1552082A JP S6154352 B2 JPS6154352 B2 JP S6154352B2
Authority
JP
Japan
Prior art keywords
pitch
raw material
produced
heat treatment
mesophase
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
Application number
JP57015520A
Other languages
Japanese (ja)
Other versions
JPS58134176A (en
Inventor
Shozo Watabe
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.)
Kashima Oil Co Ltd
Original Assignee
Kashima Oil 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 Kashima Oil Co Ltd filed Critical Kashima Oil Co Ltd
Priority to JP1552082A priority Critical patent/JPS58134176A/en
Publication of JPS58134176A publication Critical patent/JPS58134176A/en
Publication of JPS6154352B2 publication Critical patent/JPS6154352B2/ja
Granted legal-status Critical Current

Links

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

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は高強度高弾性炭素繊維用の原料として
のメソフエーズピツチを含有するピツチの製造法
に係るもので、複合材料の原料として好適な高強
度高弾性炭素繊維を安価に短時間で製造する方法
を提供することを目的とするものである。 本発明は減圧軽油の熱接触分解(FCC)、或い
はナフサの熱分解によつて副生する残渣炭素物質
の石油系ピツチ及び石炭系タールを温度360℃乃
至420℃で加熱処理する際、加熱処理時間を短縮
し反応を円滑にするため原料ピツチ中に既に混在
する揮発留分及び加熱処理時に副生するメソフエ
ーズ生成妨害である揮発性の重質物を反応系から
除去するためにキヤリヤーガスとして非酸化性ガ
スを使用して追い出し、加熱生成ピツチ中にメソ
フエーズ留分(偏光顕微鏡で容易に測定できる)
を20%乃至60%含有する様に、非酸化性気流下で
常圧或いは加圧下で30分乃至20時間加熱処理して
メソフエーズピツチを含有する加熱生成ピツチを
製造する方法にある。 近年航空機、自動車その他の輸送機製作工業の
急速な成長の結果、それに必要な材料として特別
な物質の組合わせからなり、そのいくつかの物理
的性質が極めて勝れておつて特異性を発揮しうる
材料を望む声が大きくなつているが特に高い強度
及び弾性を具備し、同時に軽量で安価な材料の出
現が強く要求されている。しかるに現在の技術で
かかる要望にかなつた材料を末だ多量安定して供
給することが出来ないので、これに答えるための
複合物質(強化樹脂)の製造に関する研究が盛ん
に行なわれている。 強化樹脂に使用される最も有望な材料の一つと
して高強度高弾性の炭素繊維がある。この材料は
前述の産業の急速な成長が始まりかけた頃から現
われたもので、この炭素繊維を樹脂と組合わせて
使用すると、他に全く類例を見ないような特性を
発揮する強化樹脂を製造することが出来る。しか
しながら残念なことには上記の様な強化樹脂用の
高強度高弾性の炭素繊維は極めて顕著な特性を発
揮するにもかかわらず、その需要があまり開拓さ
れていない。この原因は以下述べる様に主として
製造コストが高くつくことにある。 現在入手出来る高強度高弾性の炭素繊維の原料
が特殊な製造法及び紡糸法によつて製造されたポ
リアクロニトリル繊維が主であることが知られて
いるが、このアクリル繊維は炭素繊維の前駆体と
して高価であるばかりでなく、この前駆体からの
炭素繊維の収率が45%以下で極めて悪い、このこ
とが優れた炭素繊維を製造する処理工程を複雑に
し、最終製品の炭素繊維の製造コストを益々高め
ることになつている。 高強度高弾性炭素繊維を安価に製造する方法と
して、40%乃至90%のメソフエーズを含有するピ
ツチから製造する方法が米国特許4005183号に記
載されており、メソフエーズが高強度高弾性炭素
繊維用の原料として優れた原料であることは公知
である。又特開昭53―86717号の公報に記載され
ている様に不活性ガスとして窒素、アルゴンキセ
ノン、ヘルミウム、スチーム等を使用して、メソ
フエーズを含有するピツチを製造することも公知
の事実である。しかしかゝる公知の高強度高弾性
炭素繊維を製造する方法は製造コストがいずれも
高い。上製造に時間がかゝる。 本願発明者は研究を実施した結果、極めて安価
な石油系及びタール系ピツチを原料として20%乃
至60%のメソフエーズを含有する加熱生成ピツチ
を製造する場合原料を360℃乃至420℃に加熱処理
の原料ピツチ中に既に混在する揮発留分及び副生
する揮発性のメソフエーズ生成妨害物質を反応系
から特に効率良く迅速に除去するため、非酸化性
ガスをキヤリヤーガスとして使用し、前述の揮発
性物質を追い出して非酸化性気流下、加熱処理反
応を円滑に進めると同時に加熱処理時間を短縮し
得ることを見付けて本発明を完成した。 一般に石油系及びタール系ピツチを380℃乃至
440℃で加熱処理して好ましい量のメソフエーズ
を含有する加熱生成ピツチを製造するためには通
常2時間乃至60時間を必要とする。この時間を短
縮するため加熱処理温度として出来るだけ高めの
処理温度420℃乃至440℃を採用して処理時間も2
時間乃至20時間にすると生成されたメソフエーズ
は平均分子量が大きくなつて、妨糸性が悪くな
る。従つて妨糸性の良いメソフエーズを含有する
ピツチを製造するための好ましい加熱温度は390
℃乃至410℃で、この温度条件では加熱時間は6
時間乃至40時間を必要とする。しかしこの温度条
件で非酸化性ガスを2乃至10/Kg分使用して加
熱処理して原料中既に混在する揮発留分及びメソ
フエーズ生成のためには妨害となる揮発性の副生
留分を選択的に効率良く反応系から除去すると加
熱時間を2時間乃至6時間程度に極めて短縮し得
ると同時に反応を円滑に進めることができる。 尚、非酸化性ガスとして使用出来るものは、上
記の加熱処理条件下でキヤリヤーガスとしてその
性能を発揮出来るものであるが、メタン、エタ
ン、プロパン、ブタン等炭素数の少ない炭化水素
沸点が低く重質化しないナフサ留分等であるが経
済的に最も優れているガスとしては原料を加熱処
理して副生するドライガス(主として炭素数の少
ない炭化水素の混合物)を挙げることができる。
しかも非酸化性ガスは特開昭53―86717の不活性
ガスの場合に比較して、その理由は良くわかつて
いないが(多分原料ピツチとのなじみと考えられ
るが)ガスの使用量が少なくなり処理時間が短く
なることが判明した。メソフエーズの含有量の分
析はキノリン不溶分(Q1)で実測し、キノリン
可溶分(QS)はキノリン(80℃)によつて測定
した。 実施例 1 減圧軽油の熱接触分解(FCC)によつて副生
されるB.P.380℃〜384℃以上の残渣炭素物質を非
酸化性気流下で400℃に2時間加熱処理し、前駆
体ピツチを製造し更らにこの前駆体を次の加熱処
理条件で処理した。 前駆体の収率は54%であつた。次に得られた前
駆体を次の加熱処理条件で処理した。 尚、前駆体の製造に於て前駆体を加熱処理に使
用する非酸化性気流として加熱処理反応で副生す
るドライガスを循環使用した。
The present invention relates to a method for producing pitch containing mesophasic pitch as a raw material for high-strength, high-modulus carbon fibers, and is capable of producing high-strength, high-modulus carbon fibers suitable as raw materials for composite materials at low cost and in a short time. The purpose is to provide a method to do so. The present invention provides heat treatment when heat treating petroleum-based pitch and coal-based tar, which are residual carbon substances produced by thermal catalytic cracking (FCC) of vacuum gas oil or thermal cracking of naphtha, at a temperature of 360°C to 420°C. In order to shorten the reaction time and make the reaction smooth, a non-oxidizing carrier gas is used to remove from the reaction system volatile fractions already mixed in the raw material pitch and volatile heavy substances that are by-products during heat treatment that interfere with mesophase formation. Mesophase fraction (easily measured with polarized light microscopy) is generated in the heated pitch by expelling it using gas.
The method is to produce a heat-generated pitch containing mesophasic pitch by heat-treating it under a non-oxidizing air flow at normal pressure or under pressure for 30 minutes to 20 hours so that the mesophase pitch contains 20% to 60% of mesophasic pitch. As a result of the rapid growth of the aircraft, automobile, and other transportation manufacturing industries in recent years, the materials required for them are made up of special combinations of substances, some of which have extremely superior physical properties and exhibit unique properties. There has been an increasing demand for materials that have high strength and elasticity, and there is a strong demand for materials that are lightweight and inexpensive at the same time. However, with the current technology, it is still not possible to stably supply materials that meet these demands in large quantities, and therefore research is being actively conducted on the production of composite materials (reinforced resins) to meet this demand. One of the most promising materials for use in reinforced resins is high-strength, high-modulus carbon fiber. This material appeared at the beginning of the rapid growth of the aforementioned industry, and when used in combination with resins, the carbon fibers produced reinforced resins with properties that were completely unparalleled. You can. Unfortunately, however, the demand for high-strength, high-elastic carbon fibers for use in reinforced resins as described above has not been fully exploited, even though they exhibit extremely remarkable properties. The main reason for this is the high manufacturing cost, as described below. It is known that the raw material for currently available high-strength, high-elastic carbon fibers is mainly polyacronitrile fibers produced using special manufacturing and spinning methods. In addition to being expensive as a carbon fiber, the yield of carbon fiber from this precursor is extremely poor at less than 45%, which complicates the processing steps to produce superior carbon fiber and hinders the production of the final carbon fiber. This is leading to increased costs. As a method for producing high-strength, high-modulus carbon fibers at low cost, a method for producing them from pitch containing 40% to 90% mesophase is described in U.S. Patent No. 4005183. It is known that it is an excellent raw material. It is also a known fact that mesophase-containing pitches can be produced using nitrogen, argon xenon, helmium, steam, etc. as inert gases, as described in JP-A-53-86717. . However, all of the known methods for producing high-strength, high-modulus carbon fibers are expensive to produce. Manufacturing takes time. As a result of research, the inventor of the present application has found that when producing heat-generated pitch containing 20% to 60% mesophase using extremely cheap petroleum-based or tar-based pitch as a raw material, the raw material must be heated to 360°C to 420°C. In order to remove the volatile fraction already mixed in the raw material pitch and the volatile by-products that interfere with mesophase production from the reaction system in a particularly efficient and rapid manner, a non-oxidizing gas is used as a carrier gas to remove the volatile substances mentioned above. The present invention was completed based on the discovery that the heat treatment reaction could proceed smoothly under a non-oxidizing gas flow by expelling the heat treatment, and at the same time, the heat treatment time could be shortened. Generally, petroleum-based and tar-based pitches are heated to 380°C or more.
Heat treatment at 440° C. typically requires 2 to 60 hours to produce a heat-produced pitch containing the preferred amount of mesophase. In order to shorten this time, we adopted a heat treatment temperature as high as possible, 420℃ to 440℃, and the treatment time was also reduced to 2.
If the heating time is increased to 20 hours, the average molecular weight of the produced mesophase becomes large and the anti-threading properties become poor. Therefore, the preferred heating temperature for producing mesophase-containing pitches with good thread blocking properties is 390°C.
℃ to 410℃, the heating time is 6 at this temperature condition.
It takes between 40 hours and 40 hours. However, under these temperature conditions, heat treatment using 2 to 10/Kg of non-oxidizing gas selects volatile fractions already mixed in the raw material and volatile by-product fractions that interfere with mesophase production. If it is efficiently removed from the reaction system, the heating time can be extremely shortened to about 2 to 6 hours, and at the same time the reaction can proceed smoothly. Non-oxidizing gases that can be used are those that can demonstrate their performance as carrier gas under the above heat treatment conditions, but hydrocarbons with a small number of carbon atoms, such as methane, ethane, propane, and butane, and heavy gases with low boiling points, The most economically advantageous gas is dry gas (mainly a mixture of hydrocarbons with a small number of carbon atoms) produced as a by-product by heat-treating raw materials.
Moreover, compared to the inert gas used in JP-A-53-86717, non-oxidizing gas requires less gas, although the reason for this is not well understood (probably due to its compatibility with the raw material pitch). It was found that the processing time was shortened. The content of mesophase was measured using quinoline insoluble content (Q1), and quinoline soluble content (QS) was measured using quinoline (80°C). Example 1 Residual carbon material with a BP of 380°C to 384°C or higher produced by thermal catalytic cracking (FCC) of vacuum gas oil was heat-treated at 400°C for 2 hours under a non-oxidizing air flow to produce a precursor pitch. Furthermore, this precursor was treated under the following heat treatment conditions. The yield of precursor was 54%. Next, the obtained precursor was treated under the following heat treatment conditions. In the production of the precursor, a dry gas produced as a by-product in the heat treatment reaction was circulated and used as a non-oxidizing gas stream used in the heat treatment of the precursor.

【表】【table】

【表】 実施例 2 ナフサの熱分解によつて副生されるB.P.200℃
以上の残渣炭素物質を次の条件で処理した。尚、
非酸化性気流としてプロパンガスを利用した。
[Table] Example 2 BP200℃ produced by thermal decomposition of naphtha
The above residual carbon material was treated under the following conditions. still,
Propane gas was used as the non-oxidizing gas stream.

【表】【table】

【表】【table】

【表】 ×分
[Table] × minutes

Claims (1)

【特許請求の範囲】[Claims] 1 石油系又はタール系ピツチをキヤリヤーガス
を通気してピツチ中に混在する揮発留分を追出し
て高強度高弾性炭素繊維用の原料としてのメソフ
エーズを含有するピツチの製造法に於いて、上記
キヤリヤーガスとしてプロパン、プタン、又はそ
れらの混合物、又は沸点が低く重質化しないナフ
サ留成又は原料を加熱処理して副生する主として
炭素数の少ない炭化水素の混合物であるドライガ
スを使用して原料ピツチ中に既に混在する揮発留
分及び加熱処理中に副生する揮発留分を追い出す
ことを特徴とするメソフエーズを含有するピツチ
の製造法。
1. In a method for producing pitch containing mesophase as a raw material for high-strength, high-elastic carbon fibers by passing a carrier gas through petroleum-based or tar-based pitch to drive out volatile fractions mixed in the pitch, the above-mentioned carrier gas is used. Propane, butane, or a mixture thereof, or a naphtha distillation with a low boiling point that does not become heavy, or a dry gas that is a mixture of hydrocarbons with a low carbon number, which are by-produced by heating the raw material, is used to add it to the raw material pitch. A method for producing pitucci containing mesophase, characterized by expelling volatile fractions already mixed therein and volatile fractions produced as by-products during heat treatment.
JP1552082A 1982-02-04 1982-02-04 Preparation of pitch containing meso-phase pitch using carrier gas Granted JPS58134176A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1552082A JPS58134176A (en) 1982-02-04 1982-02-04 Preparation of pitch containing meso-phase pitch using carrier gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1552082A JPS58134176A (en) 1982-02-04 1982-02-04 Preparation of pitch containing meso-phase pitch using carrier gas

Publications (2)

Publication Number Publication Date
JPS58134176A JPS58134176A (en) 1983-08-10
JPS6154352B2 true JPS6154352B2 (en) 1986-11-21

Family

ID=11891085

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1552082A Granted JPS58134176A (en) 1982-02-04 1982-02-04 Preparation of pitch containing meso-phase pitch using carrier gas

Country Status (1)

Country Link
JP (1) JPS58134176A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62178867U (en) * 1986-05-01 1987-11-13

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2462369C2 (en) * 1973-12-11 1984-05-17 Union Carbide Corp., New York, N.Y. Process for the preparation of a pitch containing mesophase
US3974264A (en) * 1973-12-11 1976-08-10 Union Carbide Corporation Process for producing carbon fibers from mesophase pitch
JPS5455005A (en) * 1977-10-12 1979-05-01 Chiyoda Chem Eng & Constr Co Ltd Cracking of heavy hydrocarbons to lighter grade
US4303631A (en) * 1980-06-26 1981-12-01 Union Carbide Corporation Process for producing carbon fibers

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62178867U (en) * 1986-05-01 1987-11-13

Also Published As

Publication number Publication date
JPS58134176A (en) 1983-08-10

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