JPS58144124A - Preparation of carbon fiber using pitch - Google Patents
Preparation of carbon fiber using pitchInfo
- Publication number
- JPS58144124A JPS58144124A JP2314682A JP2314682A JPS58144124A JP S58144124 A JPS58144124 A JP S58144124A JP 2314682 A JP2314682 A JP 2314682A JP 2314682 A JP2314682 A JP 2314682A JP S58144124 A JPS58144124 A JP S58144124A
- Authority
- JP
- Japan
- Prior art keywords
- fibers
- pitch
- oxidized
- oxygen
- inert gas
- 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
Abstract
Description
【発明の詳細な説明】
本発明は、所謂ピッチ類により炭素系繊維を製造する方
法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing carbon fibers using so-called pitches.
炭素繊維の製造に際して、テトラヒドロキノリンにより
還元処理されたピッチ類によるiamは酸化による不融
化処理暗闘が短い特徴を有しているが、不融化にひき続
く炭化処理が不活性気体雰囲気中で行われるにもかかわ
らず、繊維束に含まれる微量の酸素の影響によって強度
低下が起る。In the production of carbon fibers, IAM made of pitches that have been reduced by tetrahydroquinoline has the characteristic that the infusibility treatment process due to oxidation is short, but the carbonization treatment that follows the infusibility treatment is performed in an inert gas atmosphere. Nevertheless, the strength decreases due to the influence of trace amounts of oxygen contained in the fiber bundle.
本尭明者らは、かかる欠点を改良するために鋭意検討し
た結果、酸化処理されたピッチから得られる繊維を還元
性液体中を通過させるか、および/または1100PP
未満の酸素を含む不活性気体中の通過、減圧置換を行い
、次いで酸素含有量が1100PP未満である不活性気
体中で炭化処理することによって強度が低下しない炭素
繊維を得て、本発明に到った。As a result of intensive studies to improve these drawbacks, the authors have decided to pass fibers obtained from oxidized pitch through a reducing liquid and/or to improve 1100PP.
By passing through an inert gas containing less than 1,000 PP of oxygen and replacing under reduced pressure, and then carbonizing in an inert gas with an oxygen content of less than 1,100 PP, carbon fibers with no decrease in strength were obtained, and the present invention was achieved. It was.
即ち、本発明は、テトラヒドロキノリンで還元処理され
たピッチ類より得た繊維を酸化処理したのち、酸化され
た繊維の遊離酸素含有量が1100PP未満となるよう
に該繊維を処理し、次いで酸素含有量が1100PP未
満の不活性気体中で炭化処理し、必要により黒鉛化処理
することを特徴とするピッチ類による炭素系繊維の製造
方法を提供する。That is, the present invention oxidizes fibers obtained from pitches that have been reduced with tetrahydroquinoline, then treats the oxidized fibers so that the free oxygen content is less than 1100 PP, and then Provided is a method for producing carbon-based fibers using pitches, which is characterized by carbonization treatment in an inert gas having an amount of less than 1100 PP and, if necessary, graphitization treatment.
本発明に用いられるピッチ類は例えば石油ピッチ、石炭
タールピッチ、天然アスファルト、工業生産に際して副
生されるピッチ状物等であり、テトラヒドロキノリンで
還元処理される。ピッチ類を還元処理するのに用いられ
るテトラヒドロキノリンはピッチ類の溶剤としても作用
する。このテトラヒドロキノリン還元ピッチは例えば軟
化点60〜150℃のコールタールピッチとテトラヒド
ロキノリンとを等重量混合し、溶解して、不溶分を濾過
したのち、350〜530℃で熱処理され、へに脱テト
ラヒドロキ7′リンを行い、400〜530℃で減圧上
熱処理して、軟化点200〜320℃に調製される。こ
のピッチを軟化点より20〜50℃高い温度に加熱して
、ノズル径0.5〜0.15m、紡糸速度200〜10
00m/分で紡糸すると50〜15ミクロンの繊維が得
られる。この繊維は、軟化点より約50℃低い温度で空
気中にて酸化処理され、例えば260℃、約15〜60
分の短時間で表面が酸化され不融化される。The pitches used in the present invention are, for example, petroleum pitch, coal tar pitch, natural asphalt, and pitch-like substances produced as by-products during industrial production, and are reduced with tetrahydroquinoline. Tetrahydroquinoline used to reduce pitches also acts as a solvent for pitches. This reduced tetrahydroquinoline pitch is produced by mixing equal weights of coal tar pitch with a softening point of 60 to 150°C and tetrahydroquinoline, dissolving it, filtering out insoluble matter, and then heat-treating it at 350 to 530°C to remove tetrahydroquinoline. It is heated under reduced pressure at 400-530°C to adjust its softening point to 200-320°C. This pitch is heated to a temperature 20 to 50 degrees Celsius higher than its softening point, using a nozzle diameter of 0.5 to 0.15 m and a spinning speed of 200 to 10 m.
When spinning at 00 m/min, fibers of 50-15 microns are obtained. This fiber is oxidized in air at a temperature about 50°C lower than its softening point, for example, 260°C, about 15 to 60°C.
The surface is oxidized and becomes infusible in a short period of minutes.
このような酸化処理繊維は遊離酸素を含んでおり、次の
工程である炭化処理に際しては炭素繊維劣化の原因とな
り、炭化時の態度上昇を緩やかにする必要があるため非
能率である。Such oxidized fibers contain free oxygen, which causes deterioration of the carbon fibers during the next step of carbonization, and is inefficient because it is necessary to slow down the increase in attitude during carbonization.
そこで、本発明では、かかる酸化処理された繊維を還元
性液体中を通過させるか、酸素含有量が1100PP以
下の不活性気体中を通過させるか、または減圧処理する
等によって該繊維中に含有される遊離の酸素量を110
0PP以下にする。Therefore, in the present invention, the oxidized fibers are passed through a reducing liquid, passed through an inert gas having an oxygen content of 1100 PP or less, or subjected to reduced pressure treatment to eliminate the content contained in the fibers. The amount of free oxygen is 110
Keep it below 0PP.
酸化処理繊維中の遊離酸素を1100PPにするのに周
旋に2ヶ以上の水酸基をもつ化合物力どが挙げられる。In order to reduce the free oxygen content in the oxidized fiber to 1100 PP, a compound having two or more hydroxyl groups in the oxidation treatment can be used.
こ11;:
の還元性液体はアルカリによりIIIHを9以上に調部
したものがよく、アルコール、アセトンなどで希釈され
てもよい。The reducing liquid in step 11 is preferably one in which IIIH is adjusted to 9 or more with an alkali, and may be diluted with alcohol, acetone, or the like.
又、繊維中の酸素量を減じる容易な方法としては窒素、
アルゴンなどの不活性気体中で酸化処理された繊維を容
器に入れて減圧置換する方法も行われる。尚、上記還元
性液体での処理後、不活性気体で減圧置換処理を行うこ
とは繊維中の遊離酸素を1100PP未満に調鯵するの
により効果的である。Also, an easy way to reduce the amount of oxygen in fibers is to use nitrogen,
There is also a method in which fibers that have been oxidized in an inert gas such as argon are placed in a container and replaced under reduced pressure. Note that after the treatment with the reducing liquid, performing a vacuum displacement treatment with an inert gas is more effective in controlling the free oxygen in the fibers to less than 1100 PP.
以上のようにし′て処理された繊維を1100PP以上
の酸素雰囲気にさらすことなく、1100PP未満の酸
素含有不活性気体、例えば窒素、ヘリウム、アルゴン中
で炭化、必要により黒鉛化される。The fibers treated as described above are carbonized and optionally graphitized in an oxygen-containing inert gas of less than 1100 PP, such as nitrogen, helium, or argon, without exposing them to an oxygen atmosphere of 1100 PP or more.
この際、炭化は通常、金属炉又は耐火レンガ炉等の中で
不活性ガス雰囲気下、約800〜1500℃、5〜60
分間の条件により行われる。更に、必要により行われる
黒鉛化は通常、黒鉛炉中でアルゴン又はヘリウムの雰囲
気下、約1500〜3000℃、5〜60分間の条件に
より行われる。At this time, carbonization is usually carried out in a metal furnace or a refractory brick furnace under an inert gas atmosphere at about 800 to 1500°C and 5 to 60°C.
It is carried out according to the conditions of minutes. Further, graphitization, if necessary, is usually carried out in a graphite furnace under an atmosphere of argon or helium at about 1500 to 3000° C. for 5 to 60 minutes.
本発明の方法により得られる炭素系繊維は強度、弾性率
等の物性に優れたものである。以下、実施例により本発
明を更に説明する。尚、部は重量部をあられす。The carbon fiber obtained by the method of the present invention has excellent physical properties such as strength and elastic modulus. The present invention will be further explained below with reference to Examples. In addition, parts are parts by weight.
実施例1
テトラヒドロキノリ、ンで還元処理した軟化点290℃
のピッチより紡糸した18ミクロンの繊維を空気中で2
60℃、20分間酸化処理した。この繊維をチオ硫酸ナ
トリウム12部、レゾルシン0.5部、水100部およ
び水酸化ナトリウム5部よりなる還元性液体に15分間
浸漬し、水洗した。崗、この浸漬槽は50PPMの酸素
を含む窒素ガスで置換されている。水洗後、繊維を10
鶴Hgに減圧した。Example 1 Softening point 290°C after reduction treatment with tetrahydroquinolin
18 micron fibers spun from a pitch of
Oxidation treatment was performed at 60°C for 20 minutes. The fibers were immersed for 15 minutes in a reducing liquid consisting of 12 parts of sodium thiosulfate, 0.5 parts of resorcinol, 100 parts of water, and 5 parts of sodium hydroxide, and then washed with water. In fact, this immersion tank is purged with nitrogen gas containing 50 PPM of oxygen. After washing with water, remove the fibers by 10
The pressure was reduced to Tsuru Hg.
この繊維のat、*含有量は20PPMであった。次い
で上記窒素ガスで置換された220℃の炉中で乾燥し、
同一炉で50℃/分で1500℃まで昇温して30分加
熱して炭素繊維を得た。この炭素繊維の強度は295睦
/−1弾性率は26t/wであった。The at,* content of this fiber was 20 PPM. Then dried in a 220°C oven purged with nitrogen gas,
In the same furnace, the temperature was raised to 1500°C at a rate of 50°C/min and heated for 30 minutes to obtain carbon fibers. The strength of this carbon fiber was 295 mm/-1, and the elastic modulus was 26 t/w.
陶、比較のために酸化処理後直ちに150PPMの酸素
を含有する窒素ガス雰囲気下、50℃/分で1500℃
まで昇温しで30分加熱して得た炭素繊維の強度は15
5kg/−1弾性率はx2t/l:であった。For comparison, immediately after the oxidation treatment, the temperature was 1500°C at 50°C/min in a nitrogen gas atmosphere containing 150 PPM oxygen.
The strength of carbon fiber obtained by heating for 30 minutes at a temperature of 15
5kg/-1 elastic modulus was x2t/l:.
実施例2
テトラヒドロキノリンで還元処理した軟化点250℃の
ピッチより紡糸した21ミクロン糸を用い、還元性液体
としてハイドロキノン3部と水100部の浸漬槽を用い
た以外は実施例1と同様にして炭素繊維を得た。この繊
維の強度は208kg/j、弾性率12t/−であった
。Example 2 A 21 micron yarn spun from pitch with a softening point of 250°C that had been reduced with tetrahydroquinoline was used, and a dipping bath containing 3 parts of hydroquinone and 100 parts of water as the reducing liquid was used, but in the same manner as in Example 1. Carbon fiber was obtained. The strength of this fiber was 208 kg/j, and the elastic modulus was 12 t/-.
崗、比較のために酸化処理後直ちに150PPMの酸素
を含む窒素ガス中で炭化処理した炭素繊維の強度は16
8−/−1弾性率9.81/−であった。For comparison, the strength of carbon fiber that was immediately carbonized in nitrogen gas containing 150 PPM oxygen after oxidation treatment was 16.
8-/-1 elastic modulus was 9.81/-.
特許出願人 大日本インキ化学工業株式会社財団法人
用材理化学研究所
5−Patent applicant Dainippon Ink and Chemicals Foundation
Materials Physics and Chemistry Research Institute 5-
Claims (1)
た繊維を酸化処理したのち、酸化された繊維の遊離酸素
含有量が1100PP未満となるように該繊維を処理し
、次いで酸素含有量が1100PP未満の不活性気体中
で炭化処理し、必要により黒鉛化処理することを特徴と
するピッチ類による炭素系繊維の製造方法。After oxidizing fibers obtained from pitches that have been reduced with tetrahydroquinoline, the oxidized fibers are treated so that the free oxygen content of the oxidized fibers is less than 1100 PP, and then the fibers are treated with non-oxidized fibers having an oxygen content of less than 1100 PP. A method for producing carbon-based fibers using pitches, which comprises carbonizing in an active gas and graphitizing if necessary.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2314682A JPS58144124A (en) | 1982-02-16 | 1982-02-16 | Preparation of carbon fiber using pitch |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2314682A JPS58144124A (en) | 1982-02-16 | 1982-02-16 | Preparation of carbon fiber using pitch |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58144124A true JPS58144124A (en) | 1983-08-27 |
JPS6132406B2 JPS6132406B2 (en) | 1986-07-26 |
Family
ID=12102423
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2314682A Granted JPS58144124A (en) | 1982-02-16 | 1982-02-16 | Preparation of carbon fiber using pitch |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58144124A (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63171950A (en) * | 1987-01-07 | 1988-07-15 | 株式会社アイジー技術研究所 | Outer wall and eaves ceiling receiving structure |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5135727A (en) * | 1974-09-20 | 1976-03-26 | Japan Exlan Co Ltd | Tantsuseni no seizoho |
JPS5224137A (en) * | 1975-08-20 | 1977-02-23 | Babcock Hitachi Kk | Anticorrosion method for structural steel |
JPS537537A (en) * | 1976-07-09 | 1978-01-24 | Nippon Steel Corp | Method of descaling steel wire rod |
JPS5324427A (en) * | 1976-08-18 | 1978-03-07 | Japan Exlan Co Ltd | Production of carbon fibers |
-
1982
- 1982-02-16 JP JP2314682A patent/JPS58144124A/en active Granted
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5135727A (en) * | 1974-09-20 | 1976-03-26 | Japan Exlan Co Ltd | Tantsuseni no seizoho |
JPS5224137A (en) * | 1975-08-20 | 1977-02-23 | Babcock Hitachi Kk | Anticorrosion method for structural steel |
JPS537537A (en) * | 1976-07-09 | 1978-01-24 | Nippon Steel Corp | Method of descaling steel wire rod |
JPS5324427A (en) * | 1976-08-18 | 1978-03-07 | Japan Exlan Co Ltd | Production of carbon fibers |
Also Published As
Publication number | Publication date |
---|---|
JPS6132406B2 (en) | 1986-07-26 |
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