JPS6088124A - Method for infusibilizing pitch fiber - Google Patents
Method for infusibilizing pitch fiberInfo
- Publication number
- JPS6088124A JPS6088124A JP19095283A JP19095283A JPS6088124A JP S6088124 A JPS6088124 A JP S6088124A JP 19095283 A JP19095283 A JP 19095283A JP 19095283 A JP19095283 A JP 19095283A JP S6088124 A JPS6088124 A JP S6088124A
- Authority
- JP
- Japan
- Prior art keywords
- pitch
- fibers
- dimethylpolysiloxane
- infusible
- pitch fibers
- 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.)
- Granted
Links
Landscapes
- Inorganic Fibers (AREA)
Abstract
Description
【発明の詳細な説明】 本発明はピッチ繊維の不融化方法に関する。[Detailed description of the invention] The present invention relates to a method for making pitch fibers infusible.
ピッチ系炭素繊維は、炭素質ピッチ全溶融紡糸して得ら
れるピッチ繊維を、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。ピッチ繊維の不融
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
化反応中のピッ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
。Pitch-based carbon fibers are produced by subjecting pitch fibers obtained by completely 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. The pitch fibers coalesce into each other, albeit very slightly,
When the mutually bonded infusible fibers are carbonized or further graphitized, the splitting properties of the resulting carbon fibers are reduced.
本発明の目的は、ピッチ繊維間の合着を防止し、分繊性
のすぐれた炭素繊維を製造することにある。An object of the present invention is to prevent coalescence between pitch fibers and to produce carbon fibers with excellent splitting properties.
前記本発明の目的は、炭素質ピッチを溶融紡糸して得ら
れるピッチ繊維を酸化性ガス雰−気下に不融化処理する
方法において、ピッチ線維に250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
した後、不融化することにより達成される。The object of the present invention is to provide a method in which pitch fibers obtained by melt-spinning carbonaceous pitch are rendered infusible in an oxidizing gas atmosphere, such that the pitch fibers have a viscosity of 0.25%.
This is achieved by applying dimethylpolysiloxane having a strength of 5 to 500 cSt and then making it infusible.
ピッチ繊維に油剤を付与した後、不融化処理することは
知られておシ、例えば水溶性界面活性剤の水溶液を用い
てピッ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ッチ線維とが相互に作用し、かえっ
て分繊性を低下させる。It is known that pitch fibers are treated to be infusible after being coated with an oil agent; for example, a technique has been reported in which pitch fiber bundles are bundled using an aqueous solution of a water-soluble surfactant (Japanese Patent Publication No. 1986-- No. 12740). However, when these water-soluble surfactants are used, although the convergence 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, resulting in fiber splitting. Decreases sex.
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51−127
39号)、これ會このままピッ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
、ピッ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
明の完成に至つ友。On the other hand, there are reports that silicone oils are effective in thermally stabilizing polyacrylonitrile precursors (JP-A-54-131032, JP-B-Sho 51-127).
No. 39), excellent effects cannot be obtained even if this method is applied to pitch fibers as is. The present inventors have found that a silicone compound with a limited structure and limited viscosity is extremely suitable for infusible pitch fibers, and that the obtained infusible fibers have good splitting properties. A friend who was able to discover and complete the present invention.
以下に本発明を詳述する。The present invention will be explained in detail below.
本発明に用いる炭素質ピッチとしてはコールタールピッ
チ、SRCなどの石炭系ピッチ、エチレンタールピッチ
、デカントオイルピッチ等の石油系ピッチあるいは合成
ピッチなど各種のピッチを包含するが、特に石油系ピッ
チが好ましい。The carbonaceous pitch used in the present invention includes various pitches such as coal tar pitch, coal-based pitch such as SRC, petroleum-based pitch such as ethylene tar pitch, and decant oil pitch, or synthetic pitch, but petroleum-based pitch is particularly preferred. .
前記ピッチを変性したもの、例えばテトラリンなどの水
素供与物で処理したもの、20〜350〜/dの水素加
圧下に水素化したもの、熱処理によシ改質したもの、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
の各種変性ピッチも本発明でいう炭素質ピッチである。The above pitch is modified, for example, treated with a hydrogen donor such as tetralin, hydrogenated under a hydrogen pressure of 20 to 350/d, modified by heat treatment, or modified by these methods as appropriate. Various modified pitches, such as those modified in combination, are also carbonaceous pitches as used in the present invention.
す々わち、本発明の炭素質ピッチとはピッチ繊維を形成
し得る前駆体ピッチを総称する意味に用いられる。In other words, the carbonaceous pitch of the present invention is used to collectively refer to precursor pitch that can form pitch fibers.
本発明の炭素質ピッチは、光学的に等方性のピッチであ
ってもよいし、また光学的に異方性のピッチであっても
よい。The carbonaceous pitch of the present invention may be an optically isotropic pitch or an optically anisotropic pitch.
光学的に等方性のピッチである場合、反射率が9.0〜
11.〇−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ッチを包埋せ
しめたのち研磨し、反射率測定装置によシ空気中にて測
定される。When the pitch is optically isotropic, the reflectance is 9.0~
11. Those exhibiting values within the range of - are preferred. Here, the reflectance is measured by embedding pitch in a resin such as acrylic resin, polishing it, and measuring it in air using a reflectance measuring device.
光学的に異方性のピッチとは、ピッ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〜
450Cにて加熱処理含有うことにより得られる光学的
異方性相(いわゆるメンフェース)を含有するピッチで
あり、特にメンフェース含量が5〜100チのものが好
ましい。Optically anisotropic pitch means that the pitch is usually heated to 340 to
It is a pitch containing an optically anisotropic phase (so-called membrane phase) obtained by heat treatment at 450C, and one having a membrane phase content of 5 to 100 degrees is particularly preferable.
本発明に用いる炭素質ピッチは軟化点が240〜400
℃のものが好ましく、260〜300℃のものが特に好
ましい。The carbonaceous pitch used in the present invention has a softening point of 240 to 400.
℃ is preferable, and 260 to 300℃ is particularly preferable.
ピッチ線維は前記炭素質ピッチ全公知の方法にて溶融紡
糸を行うことにエリ得られる。例えば、炭素質ピッチを
その軟化点エリも30〜80℃高い温度にて溶融し、直
径0.1〜0.5箇のノズルから押し出しながら100
〜2000m/分で巻き取ることに工りピッチ繊維を得
る。The pitch fibers can be obtained by melt-spinning the carbonaceous pitch using a known method. For example, carbonaceous pitch is melted at a temperature 30 to 80°C higher than its softening point and extruded through a nozzle with a diameter of 0.1 to 0.5.
A machined pitch fiber is obtained by winding at ~2000 m/min.
このようにして得られたピッチ繊維に対し、25℃にお
ける粘度が0.5〜500 cstであるジメチルポリ
シロキサン全付与する。ここでいうジメチルポリシロキ
サンとは下記の構造5−
を有するものであ択好ましくは25℃における粘度が1
.0〜100 cst 、より好ましくは1.0〜25
cstのものである。A dimethylpolysiloxane having a viscosity of 0.5 to 500 cst at 25°C is applied to the pitch fiber thus obtained. The dimethylpolysiloxane mentioned here has the following structure 5-, and preferably has a viscosity of 1 at 25°C.
.. 0-100 cst, more preferably 1.0-25
It is from cst.
ジメチルポリシロキサンの粘度はきわめて重要であり、
粘度が上記範囲工)大きい場合には、不融化反応の障害
となシ、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。The viscosity of dimethylpolysiloxane is extremely important;
If the viscosity is high within the above range, the infusibility reaction will be hindered and the infusibility rate will decrease. 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.
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。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.
このほか、シリコーン系としては、メチルフェニルポリ
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)、フッ
素変性物、6一
アミノ変性物などが知られているが、これらのいずれも
不融化中にピッチ繊維と相互に作用し、分繊性全低下さ
せることが明らかとなった。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っても
、これを乳化したものは、分線性の低下を招くため好ま
しくない。Other known silicone-based materials include methylphenyl polysiloxane, methylhydrodiene polysiloxane, polyether-modified products (with increased solubility in water), fluorine-modified products, and 6-amino-modified products. However, it has become clear that all of these interact with pitch fibers during infusibility, resulting in a total decrease in fiber splitting properties. Further, even if dimethylpolysiloxane has a viscosity within the same range as that of the present invention, emulsifying it is not preferable because it causes deterioration in line segmentability.
ジメチルポリシロキサンの付与量は、ピッチ繊維に対し
て0.01〜50重量%であり、好ましくは0.1〜2
5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−1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。The amount of dimethylpolysiloxane applied is 0.01 to 50% by weight, preferably 0.1 to 2% by weight based on the pitch fiber.
It is 5% by weight. Further, the application method is not particularly limited, and known techniques such as oiling roller 1 application, dipping, and spraying can be used.
ジメチルポリシロキサンを付与したピッチ繊維は次に酸
化性ガス雰囲気下にて不融化処理される。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、よシ好ましくは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、ピッチ繊維の融着あ
るいは消耗といつ友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晶ゲン等の酸化性ガスを1
種あるいは2種以上用いる。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°C or lower.
The temperature is 380°C, preferably 200 to 350°C. If the processing temperature is too low, the processing time will be longer;
Furthermore, if the processing temperature is too high, it is not preferable because it may cause fusing or consumption of the pitch fibers. As the oxidizing gas, oxidizing gases such as oxygen, ozone, air, nitrogen oxides, sulfur dioxide gas, or halogen are usually used.
A species or two or more species are used.
不融化処理されたピッチ繊維は、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。The infusible pitch fibers are then subjected to carbonization treatment or further graphitization treatment in an inert gas atmosphere to obtain carbon fibers.
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2000〜350
0℃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Th1−
けておくこともできる。Carbonization treatment is usually carried out at a temperature of 800 to 2000°C, and the treatment time generally required for carbonization is 0.1 minute to 10 hours. When further graphitizing, the temperature is 2000 to 350.
It is usually carried out for 1 second to 1 hour at 0°C. In addition, during carbonization or graphitization, if necessary, a slight load or tension Th1-
You can also leave it there.
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。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.
実施例 1゜
光学的異方性相に80wt%含有し、軟化点が280℃
である石油系前駆体ピッチを溶融紡糸し、平均糸径13
μのピッチ繊維を得た。このピッチ繊維に、粘度4.0
cst @ 25℃のジメチルポリシロキサン10w
tq6tl−塗布し、酸素中、250℃で30分処理し
て不融化繊維を得友。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った。Example 1: Contains 80 wt% in the optically anisotropic phase and has a softening point of 280°C
The petroleum-based precursor pitch is melt-spun, and the average yarn diameter is 13
μ pitch fibers were obtained. This pitch fiber has a viscosity of 4.0
cst @ 25℃ dimethylpolysiloxane 10w
tq6tl-coated and treated in oxygen at 250°C for 30 minutes to obtain infusible fibers. The obtained infusible fiber had extremely excellent splitting properties.
比較例 1〜6
実施例1におけるピッチ繊維に、表1に示す各種シリコ
ーン系油剤10wt16f付与し、酸素中、250℃で
30分処理して不融化繊維を得た。Comparative Examples 1 to 6 The pitch fibers in Example 1 were applied with 10wt16f of various silicone oils shown in Table 1, and treated in oxygen at 250°C for 30 minutes to obtain infusible fibers.
表1
比較例1 ジメチルポリシロキサン 1ρ00cSt
△12 1 100ρ0OcSt X
〃 3 メチルフェニルポリシロキサ7 500cSt
xl 4 アミノ変性シロキサン 1,200cSt
xI 5 フッ素変性シロキサン 300 cst x
l 6 ジメチルポリシロキサン乳化物 40cSt
X9−
比較例1〜2はジメチルポリシロキサンで高粘度のもの
、比較例3〜5は変性シリコーン、比較例6はジメチル
ポリシロキサンの乳化物であり、いずれの場合も分繊性
のすぐれた不融化繊維は得られなかった。Table 1 Comparative Example 1 Dimethylpolysiloxane 1ρ00cSt
△12 1 100ρ0OcSt X 〃 3 Methylphenyl polysiloxa 7 500cSt
xl 4 Amino modified siloxane 1,200cSt
xI 5 Fluorine modified siloxane 300 cst x
l 6 Dimethylpolysiloxane emulsion 40cSt
X9- Comparative Examples 1 and 2 are dimethylpolysiloxane with high viscosity, Comparative Examples 3 and 5 are modified silicone, and Comparative Example 6 is a dimethylpolysiloxane emulsion, and in each case, a nonwoven material with excellent fibrillation properties is used. No fused fibers were obtained.
実施例 2〜6
反射率10.3%、軟化点260’Cの光学的に等方性
の石油系前駆体ピッチを溶融紡糸し、平均糸径12μの
ピッチ繊維を得た。このピッチ繊維に、表2に示すジメ
チルポリシロキサンを付与し、酸素中2℃/mで280
t:まで昇温し不融化繊維を得た。これらの不融化繊維
の分繊性を表2に併せて示す。Examples 2 to 6 Optically isotropic petroleum precursor pitch having a reflectance of 10.3% and a softening point of 260'C was melt-spun to obtain pitch fibers with an average yarn diameter of 12μ. Dimethylpolysiloxane shown in Table 2 was added to this pitch fiber, and the pitch fiber was heated at 280 °C/m in oxygen.
The temperature was raised to t: to obtain infusible fibers. Table 2 also shows the splitting properties of these infusible fibers.
表1及び表2において○は優れる、△は普通、×は劣る
全意味する。In Tables 1 and 2, ◯ means excellent, △ means average, and × means poor.
10−10-
Claims (1)
性ガス雰囲気下に不融化処理する方法において、ピッチ
繊維に25℃における粘度が0,5〜500 cStで
あるジメチルポリシロキサンを付与した後、不融化する
ことを特徴とするピッチ繊維の不融化方法。In a method of infusibleizing pitch fibers obtained by melt-spinning carbonaceous pitch in an oxidizing gas atmosphere, after imparting dimethylpolysiloxane having a viscosity of 0.5 to 500 cSt at 25° C. to pitch fibers, A method for making pitch fiber infusible, characterized by making it infusible.
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 true JPS6088124A (en) | 1985-05-17 |
JPH041087B2 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) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4656022A (en) * | 1985-01-18 | 1987-04-07 | Nippon Oil Company, Limited | Process for producing pitch carbon fibers |
US4923692A (en) * | 1986-06-12 | 1990-05-08 | Mitsubishi Kasei Corporation | Process for producing pitch-type carbon fibers |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5188729A (en) * | 1974-12-24 | 1976-08-03 | ||
JPS52148227A (en) * | 1976-05-10 | 1977-12-09 | Mitsubishi Rayon Co Ltd | Preparation of carbon fiber from acrylic fiber |
JPS54131032A (en) * | 1978-03-27 | 1979-10-11 | Mitsubishi Rayon Co Ltd | Production of carbon fibers from acrylic fibers |
JPS54134126A (en) * | 1978-04-11 | 1979-10-18 | Nippon Kainooru Kk | Production of carbon fiber or carbon fiber structure with excellent heat resistance |
JPS55128020A (en) * | 1979-01-29 | 1980-10-03 | Union Carbide Corp | Treating of multi filament bundle of pitch fiber and finishing composition |
-
1983
- 1983-10-14 JP JP19095283A patent/JPS6088124A/en active Granted
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5188729A (en) * | 1974-12-24 | 1976-08-03 | ||
JPS52148227A (en) * | 1976-05-10 | 1977-12-09 | Mitsubishi Rayon Co Ltd | Preparation of carbon fiber from acrylic fiber |
JPS54131032A (en) * | 1978-03-27 | 1979-10-11 | Mitsubishi Rayon Co Ltd | Production of carbon fibers from acrylic fibers |
JPS54134126A (en) * | 1978-04-11 | 1979-10-18 | Nippon Kainooru Kk | Production of carbon fiber or carbon fiber structure with excellent heat resistance |
JPS55128020A (en) * | 1979-01-29 | 1980-10-03 | Union Carbide Corp | Treating of multi filament bundle of pitch fiber and finishing composition |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4656022A (en) * | 1985-01-18 | 1987-04-07 | Nippon Oil Company, Limited | Process for producing pitch carbon fibers |
US4923692A (en) * | 1986-06-12 | 1990-05-08 | Mitsubishi Kasei Corporation | Process for producing pitch-type carbon fibers |
Also Published As
Publication number | Publication date |
---|---|
JPH041087B2 (en) | 1992-01-09 |
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JPH04272235A (en) | Production of pitch-base carbon fiber and graphite fiber |