JPH041087B2 - - Google Patents

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Publication number
JPH041087B2
JPH041087B2 JP58190952A JP19095283A JPH041087B2 JP H041087 B2 JPH041087 B2 JP H041087B2 JP 58190952 A JP58190952 A JP 58190952A JP 19095283 A JP19095283 A JP 19095283A JP H041087 B2 JPH041087 B2 JP H041087B2
Authority
JP
Japan
Prior art keywords
pitch
fibers
infusible
present
viscosity
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
JP58190952A
Other languages
Japanese (ja)
Other versions
JPS6088124A (en
Inventor
Seiichi Kamimura
Takao Hirose
Yoshiho Hayata
Kenji Kato
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.)
Eneos Corp
Original Assignee
Nippon Oil 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 Nippon Oil Corp filed Critical Nippon Oil Corp
Priority to JP19095283A priority Critical patent/JPS6088124A/en
Publication of JPS6088124A publication Critical patent/JPS6088124A/en
Publication of JPH041087B2 publication Critical patent/JPH041087B2/ja
Granted legal-status Critical Current

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Description

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

本発明はピツチ繊維の不融化方法に関する。 ピツチ系炭素繊維は、炭素質ピツチを溶融紡糸
して得られるピツチ繊維を、不融化、炭化あるい
はさらに黒鉛化処理することにより製造されてい
る。ピツチ繊維の不融化処理は、通常400℃以下
において、酸化性ガス、例えば空気、酸素、オゾ
ン、窒素酸化物、ハロゲンあるいは亜硫酸ガスな
どの存在下で行われるが、この際、不融化反応中
のピツチ繊維がごく軽微ながら相互に合着し、こ
の相互合着した不融化繊維を炭化あるいはさらに
黒鉛化した場合には、得られる炭素繊維の分繊性
が低下する。 本発明の目的は、ピツチ繊維間の合着を防止て
分繊性を向上させ、もつて分繊性のすぐれた炭素
繊維を製造することにある。 前記本発明の目的は、炭素質ピツチを溶融紡糸
して得られるピツチ繊維を酸化性ガス雰囲気下に
不融化処理する方法において、ピツチ繊維に25℃
における粘度が0.5〜500cStであるジメチルポリ
シロキサンの非乳化物を付与した後、不融化する
ことにより達成される。 ピツチ繊維に油剤を付与した後、不融化処理す
ることは知られており、例えば水溶性界面活性剤
の水溶性を用いてピツチ繊維束を集束させる技術
が報告されている(特公昭51−−12740号)。しか
しながらこれら水溶性界面活性剤を用いる場合に
は、繊維束の集束性は向上するものの、これらを
不融化処理する場合に、高温において界面活性剤
とピツチ繊維とが相互に作用し、かえつて分繊性
を低下させる。 一方、ポリアクリルニトリル系プレカーサーの
熱安定化においてシリコーン系油剤が有効である
との報告もあるが(特開昭54−131032号、特公昭
51−12739号)、これをこのままピツチ繊維に適用
しても優れた効果を得ることはできない。本発明
者らは、限られた構造で、かつ限られた粘度を有
するシリコーン化合物が、ピツチ繊維の不融化に
きわめて好適であり、得られた不融化繊維の分繊
性が良好であることを見いだし、本発明の完成に
至つた。 以下に本発明を詳述する。 本発明に用いる炭素質ピツチとしてはコールタ
ールピツチ、SRCなどの石炭系ピツチ、エチレ
ンタールピツチ、デカントオイルピツチ等の石油
系ピツチあるいは合成ピツチなど各種のピツチを
包含するが、特に石油系ピツチが好ましい。 前記ピツチを変性したもの、例えばテトラリン
などの水素供与物で処理したもの、20〜350Kg/
cm2の水素加圧下に水素化したもの、熱処理により
改質したもの、あるいはこれらの方法を適宜組み
合わせて改質したもの等の各種変性ピツチも本発
明でいう炭素質ピツチである。 すなわち、本発明の炭素質ピツチとはピツチ繊
維を形成し得る前駆体ピツチを総称する意味に用
いられる。 本発明の炭素質ピツチは、光学的に等方性のピ
ツチであつてもよいし、また光学的に異方性のピ
ツチであつてもよい。 光学的に等方性のピツチである場合、反射率が
9.0〜11.0%の範囲内の値を示すものが好ましい。
ここで反射率とは、アクリル樹脂等の樹脂中にピ
ツチを包埋せしめたのち研磨し、反射率測定装置
により空気中にて測定される。 光学的に異方性のピツチとは、ピツチを常圧も
しくは減圧下に窒素等の不活性ガスを通気しなが
ら通常340〜450℃にて加熱処理を行うことにより
得られる光学的異方性(いわゆるメソフエース)
を含有するピツチであり、特にメソフエース含量
が5〜100%のものが好ましい。 本発明に用いる炭素質ピツチは軟化点が240〜
400℃のものが好ましく、260〜300℃のものが特
に好ましい。 ピツチ繊維は前記炭素質ピツチを公知の方法に
て溶融紡糸を行うことにより得られる。例えば、
炭素質ピツチをその軟化点よりも30〜80℃高い温
度にて溶融し、直径0.1〜0.5mmのノズルから押し
出しながら100〜200m/分で巻き取ることにより
ピツチ繊維を得る。 このようにして得られたピツチ繊維に対し、25
℃における粘度が0.5〜500cStであるジメチルポ
リシロキサンを付与する。ここでいうジメチルポ
リシロキサンとは下記の構造を有するものであ
り、好ましくは25℃における粘度が1.0〜100cSt、
より好ましくは1.0〜25cStのものである。 ジメチルポリシロキサンの粘度はきわめて重要
であり、粘度が上記範囲より大きい場合には、不
融化反応の障害となり、不融化速度が低下する。
一方、粘度が上記範囲に満たない場合には、不融
化後の繊維の分繊性が低下し、本発明の効果が期
待できない。 また2種以上のジメチルポリシロキサンの混合
物である場合、混合物としての粘度が上記範囲に
含まれるものは使用可能である。 このほか、シリコーン系としては、メチルフエ
ニルポリシロキサン、メチルハイドロジエンポリ
シロキサン、ポリエーテル変性物(水への溶解性
を高めたもの)、フツ素変性物、アミノ変性物な
どが知られているが、これらのいずれも不融化中
にピツチ繊維と相互に作用し、分繊性を低下させ
ることが明らかとなつた。またジメチルポリシロ
キサンで粘度が本発明と同じ範囲に含まれるもの
であつても、これを乳化したものは、分繊性の低
下を招くため好ましくなく本発明から除外され
る。 ジメチルポリシロキサンの付与量は、ピツチ繊
維に対して0.01〜50重量%であり、好ましくは
0.1〜25重量%である。また付与方法は特に制限
されず、オイリングローラー、塗布、浸漬あるい
はスプレーなど公知の技術が利用できる。 ジメチルポリシロキサンを付与したピツチ繊維
は次に酸化性ガス雰囲気下に不融化処理される。
不融化処理は通常400℃以下において行われ、好
ましくは150〜380℃であり、より好ましくは200
〜350℃である。処理温度が低すぎる場合には処
理時間が長くなり、また処理温度が高すぎる場合
には、ピツチ繊維の融着あるいは消耗といつた現
象を生ずるため好ましくない。酸化性ガスとして
は、通常、酸素、オゾン、空気、窒素酸化物、亜
硫酸ガスあるいはハロゲン等の酸化性ガスを1種
あるいは2種以上用いる。 不融化処理されたピツチ繊維は、次に不活性ガ
ス雰囲気下で炭化処理あるいは更に黒鉛化処理を
行い、炭素繊維を得る。炭化処理は通常、温度
800〜2000℃で行う。一般には炭化に要する処理
時間は0.1分〜10時間である。さらに黒鉛化を行
う場合には、温度2000〜3500℃で、通常1秒〜1
時間行う。また、炭化処理あるいは黒鉛化処理の
際、必要であれば収縮や変形等を防止する目的
で、被処理体に若干の荷重あるいは張力をかけて
おくこともできる。 以下に実施例および比較例をあげ本発明を具体
的に説明するが、本発明はこれら実施例に制限さ
れるものではない。 実施例 1 光学的異方性相を80wt%含有し、軟化点が280
℃である石油系前駆体ピツチを溶融紡糸し、平均
糸径13μのピツチ繊維を得た。このピツチ繊維
に、粘度4.0cSt25℃のジメチルポリシロキサン
10wt%を塗布し、酸素中、250℃で30分処理して
不融化繊維を得た。得られた不融化繊維はきわめ
て分繊性に優れたものであつた。 比較例 1〜6 実施例1におけるピツチ繊維に、表1に示す各
種シリコーン系油剤10wt%を付与し、酸素中、
250℃で30分処理して不融化繊維を得た。
The present invention relates to a method for making pitch fiber infusible. Pitch-based carbon fibers are produced by subjecting pitch fibers obtained by melt-spinning carbonaceous pitch to infusibility, carbonization, or further graphitization. The infusibility treatment of pitch fibers is usually carried out at temperatures below 400°C in the presence of oxidizing gases such as air, oxygen, ozone, nitrogen oxides, halogens, or sulfur dioxide gas. If pitch fibers coalesce with each other, albeit very slightly, and the mutually coalesced infusible fibers are carbonized or further graphitized, the splitting properties of the resulting carbon fibers will be reduced. An object of the present invention is to prevent coalescence between pitch fibers and improve splitting properties, thereby producing carbon fibers with excellent splitting properties. The object of the present invention is to provide a method for infusibility treatment of pitch fiber obtained by melt spinning carbonaceous pitch in an oxidizing gas atmosphere.
This is achieved by applying a non-emulsified dimethylpolysiloxane having a viscosity of 0.5 to 500 cSt and then making it infusible. It is known that after applying an oil agent to pitch fibers, they are treated to make them infusible. For example, a technique has been reported to bundle pitch fiber bundles using the water solubility of a water-soluble surfactant. No. 12740). However, when these water-soluble surfactants are used, although the cohesiveness of the fiber bundles is improved, when they are treated to make them infusible, the surfactants and pitch fibers interact with each other at high temperatures, and on the contrary, they become separated. Decreases fineness. On the other hand, there are reports that silicone oils are effective in thermally stabilizing polyacrylonitrile precursors (JP-A No. 54-131032,
No. 51-12739), and even if this is applied as is to pitch fibers, excellent effects cannot be obtained. The present inventors have found that a silicone compound with a limited structure and limited viscosity is extremely suitable for infusible fibers, and that the resulting infusible fibers have good splitting properties. This discovery led to the completion of the present invention. The present invention will be explained in detail below. The carbonaceous pitch used in the present invention includes various pitches such as coal-based pitch such as coal tar pitch and SRC, petroleum-based pitch such as ethylene tar pitch and decant oil pitch, or synthetic pitch, but petroleum-based pitch is particularly preferred. . The above pitch is modified, for example, treated with a hydrogen donor such as tetralin, 20-350 kg/
Various modified pitches such as those hydrogenated under hydrogen pressure of cm 2 , modified by heat treatment, or modified by an appropriate combination of these methods are also considered carbonaceous pitches in the present invention. That is, the carbonaceous pitch of the present invention is used to collectively refer to precursor pitches capable of forming pitch fibers. The carbonaceous pitch of the present invention may be an optically isotropic pitch or an optically anisotropic pitch. When the pitch is optically isotropic, the reflectance is
Those exhibiting a value within the range of 9.0 to 11.0% are preferred.
Here, the reflectance is measured by embedding a pitch in a resin such as acrylic resin, polishing it, and measuring it in air using a reflectance measuring device. Optically anisotropic pitch is an optically anisotropic pitch obtained by heat-treating pitch, usually at 340 to 450°C while passing an inert gas such as nitrogen under normal pressure or reduced pressure. so-called mesophace)
A pitch containing 5 to 100% mesophace is particularly preferred. The carbonaceous pitch used in the present invention has a softening point of 240~
A temperature of 400°C is preferred, and a temperature of 260 to 300°C is particularly preferred. Pitch fibers can be obtained by melt spinning the carbonaceous pitch using a known method. for example,
Pitch fibers are obtained by melting carbonaceous pitch at a temperature 30 to 80°C higher than its softening point, and winding it at 100 to 200 m/min while extruding it through a nozzle with a diameter of 0.1 to 0.5 mm. For the pitch fiber thus obtained, 25
Apply dimethylpolysiloxane with a viscosity of 0.5 to 500 cSt at °C. The dimethylpolysiloxane mentioned here has the following structure, and preferably has a viscosity of 1.0 to 100 cSt at 25°C,
More preferably, it is 1.0 to 25 cSt. The viscosity of dimethylpolysiloxane is extremely important; if the viscosity is greater than the above range, it will hinder the infusibility reaction and reduce the infusibility rate.
On the other hand, if the viscosity is less than the above range, the splitting properties of the infusible fibers will decrease, and the effects of the present invention cannot be expected. Further, in the case of a mixture of two or more types of dimethylpolysiloxane, those whose viscosity as a mixture is within the above range can be used. Other known silicone-based materials include methylphenyl polysiloxane, methylhydrodiene polysiloxane, polyether-modified products (those with increased solubility in water), fluorine-modified products, and amino-modified products. However, it has become clear that all of these interact with pitch fibers during infusibility and reduce the splitting properties. Furthermore, even if dimethylpolysiloxane has a viscosity within the same range as the present invention, emulsified dimethylpolysiloxanes are not preferred and are excluded from the present invention because they result in a decrease in fiber splitting properties. The amount of dimethylpolysiloxane applied is 0.01 to 50% by weight based on the pitch fiber, preferably
It is 0.1-25% by weight. Further, the application method is not particularly limited, and known techniques such as oiling roller, coating, dipping, and spraying can be used. The pitch fibers coated with dimethylpolysiloxane are then treated to be infusible in an oxidizing gas atmosphere.
The infusibility treatment is usually carried out at a temperature of 400°C or lower, preferably 150 to 380°C, more preferably 200°C.
~350℃. If the treatment temperature is too low, the treatment time becomes long, and if the treatment temperature is too high, phenomena such as fusion or consumption of the pitch fibers occur, which is not preferable. As the oxidizing gas, one or more of oxidizing gases such as oxygen, ozone, air, nitrogen oxide, sulfur dioxide gas, or halogen are usually used. The infusible pitch fibers are then subjected to carbonization treatment or further graphitization treatment in an inert gas atmosphere to obtain carbon fibers. Carbonization usually involves temperature
Perform at 800-2000℃. Generally, the treatment time required for carbonization is 0.1 minute to 10 hours. When further graphitizing, the temperature is 2000 to 3500℃, usually 1 second to 1 hour.
Do time. Furthermore, during carbonization or graphitization, a slight load or tension may be applied to the object to be treated, if necessary, in order to prevent shrinkage, deformation, etc. EXAMPLES The present invention will be specifically explained below with reference to Examples and Comparative Examples, but the present invention is not limited to these Examples. Example 1 Contains 80wt% optically anisotropic phase and has a softening point of 280
Pitch fibers having an average diameter of 13 μm were obtained by melt-spinning petroleum precursor pitch at a temperature of 13°C. Dimethylpolysiloxane with a viscosity of 4.0cSt25℃ is added to this pitch fiber.
10wt% was applied and treated in oxygen at 250°C for 30 minutes to obtain infusible fibers. The obtained infusible fibers had extremely excellent splitting properties. Comparative Examples 1 to 6 10 wt% of various silicone oils shown in Table 1 were applied to the pitch fibers in Example 1, and the mixture was heated in oxygen.
Infusible fibers were obtained by treatment at 250°C for 30 minutes.

【表】 シロキサン
[Table] Siloxane

【表】 化物
[Table] Monster

Claims (1)

【特許請求の範囲】[Claims] 1 炭素質ピツチを溶融紡糸して得られるピツチ
繊維を酸化性ガス雰囲気下に不融化処理する方法
において、ピツチ繊維に25℃における粘度が0.5
〜500cStであるジメチルポリシロキサンの非乳化
物を付与した後、不融化することを特徴とするピ
ツチ繊維から分繊性に優れた不融化繊維を製造す
る方法。
1 In a method of infusibleizing pitch fiber obtained by melt spinning carbonaceous pitch in an oxidizing gas atmosphere, pitch fiber has a viscosity of 0.5 at 25°C.
A method for producing infusible fibers with excellent splitting properties from pitch fibers, which comprises applying a non-emulsified dimethylpolysiloxane having a weight of ~500 cSt and then infusifying the fibers.
JP19095283A 1983-10-14 1983-10-14 Method for infusibilizing pitch fiber Granted JPS6088124A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19095283A JPS6088124A (en) 1983-10-14 1983-10-14 Method for infusibilizing pitch fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19095283A JPS6088124A (en) 1983-10-14 1983-10-14 Method for infusibilizing pitch fiber

Publications (2)

Publication Number Publication Date
JPS6088124A JPS6088124A (en) 1985-05-17
JPH041087B2 true JPH041087B2 (en) 1992-01-09

Family

ID=16266405

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19095283A Granted JPS6088124A (en) 1983-10-14 1983-10-14 Method for infusibilizing pitch fiber

Country Status (1)

Country Link
JP (1) JPS6088124A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61167021A (en) * 1985-01-18 1986-07-28 Nippon Oil Co Ltd Production of pitch carbon yarn
DE3775834D1 (en) * 1986-06-12 1992-02-20 Mitsubishi Chem Ind METHOD FOR PRODUCING PECH CARBON FIBERS.

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA1055664A (en) * 1974-12-24 1979-06-05 Union Carbide Corporation Rapid thermosetting of carbonaceous fibers produced from mesophase pitch
JPS52148227A (en) * 1976-05-10 1977-12-09 Mitsubishi Rayon Co Ltd Preparation of carbon fiber from acrylic fiber
JPS6052206B2 (en) * 1978-03-27 1985-11-18 三菱レイヨン株式会社 Method for manufacturing acrylic carbon fiber
JPS54134126A (en) * 1978-04-11 1979-10-18 Nippon Kainooru Kk Production of carbon fiber or carbon fiber structure with excellent heat resistance
US4275051A (en) * 1979-01-29 1981-06-23 Union Carbide Corporation Spin size and thermosetting aid for pitch fibers

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Publication number Publication date
JPS6088124A (en) 1985-05-17

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