JPS6132406B2 - - Google Patents
Info
- Publication number
- JPS6132406B2 JPS6132406B2 JP57023146A JP2314682A JPS6132406B2 JP S6132406 B2 JPS6132406 B2 JP S6132406B2 JP 57023146 A JP57023146 A JP 57023146A JP 2314682 A JP2314682 A JP 2314682A JP S6132406 B2 JPS6132406 B2 JP S6132406B2
- Authority
- JP
- Japan
- Prior art keywords
- fibers
- ppm
- treatment
- tetrahydroquinoline
- less
- 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
Links
- 239000000835 fiber Substances 0.000 claims description 25
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 20
- 239000001301 oxygen Substances 0.000 claims description 20
- 229910052760 oxygen Inorganic materials 0.000 claims description 20
- LBUJPTNKIBCYBY-UHFFFAOYSA-N 1,2,3,4-tetrahydroquinoline Chemical compound C1=CC=C2CCCNC2=C1 LBUJPTNKIBCYBY-UHFFFAOYSA-N 0.000 claims description 18
- 239000011295 pitch Substances 0.000 claims description 12
- 239000011261 inert gas Substances 0.000 claims description 10
- 238000003763 carbonization Methods 0.000 claims description 7
- 238000004519 manufacturing process Methods 0.000 claims description 4
- 238000005087 graphitization Methods 0.000 claims description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 2
- 229910052799 carbon Inorganic materials 0.000 claims 1
- 230000001590 oxidative effect Effects 0.000 claims 1
- 229920000049 Carbon (fiber) Polymers 0.000 description 11
- 239000004917 carbon fiber Substances 0.000 description 11
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
- 125000004122 cyclic group Chemical group 0.000 description 7
- 239000007788 liquid Substances 0.000 description 7
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 6
- QIGBRXMKCJKVMJ-UHFFFAOYSA-N Hydroquinone Chemical compound OC1=CC=C(O)C=C1 QIGBRXMKCJKVMJ-UHFFFAOYSA-N 0.000 description 4
- 229910001873 dinitrogen Inorganic materials 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- GHMLBKRAJCXXBS-UHFFFAOYSA-N resorcinol Chemical compound OC1=CC=CC(O)=C1 GHMLBKRAJCXXBS-UHFFFAOYSA-N 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 229910052786 argon Inorganic materials 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- YCIMNLLNPGFGHC-UHFFFAOYSA-N catechol Chemical compound OC1=CC=CC=C1O YCIMNLLNPGFGHC-UHFFFAOYSA-N 0.000 description 2
- 239000011294 coal tar pitch Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000006073 displacement reaction Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000001307 helium Substances 0.000 description 2
- 229910052734 helium Inorganic materials 0.000 description 2
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 238000009987 spinning Methods 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 239000010426 asphalt Substances 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000011301 petroleum pitch Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- AKHNMLFCWUSKQB-UHFFFAOYSA-L sodium thiosulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=S AKHNMLFCWUSKQB-UHFFFAOYSA-L 0.000 description 1
- 235000019345 sodium thiosulphate Nutrition 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- RVEZZJVBDQCTEF-UHFFFAOYSA-N sulfenic acid Chemical compound SO RVEZZJVBDQCTEF-UHFFFAOYSA-N 0.000 description 1
- BUUPQKDIAURBJP-UHFFFAOYSA-N sulfinic acid Chemical compound OS=O BUUPQKDIAURBJP-UHFFFAOYSA-N 0.000 description 1
- DHCDFWKWKRSZHF-UHFFFAOYSA-N sulfurothioic S-acid Chemical compound OS(O)(=O)=S DHCDFWKWKRSZHF-UHFFFAOYSA-N 0.000 description 1
- 150000003530 tetrahydroquinolines Chemical class 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Description
【発明の詳細な説明】
本発明は、所謂ピツ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
ンにより環元処理されたピツチ類による繊維は酸
化による不融化処理時間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つて強度低下が起る。 During the production of carbon fibers, fibers made from pitts treated with tetrahydroquinoline have a short time for infusibility by oxidation, but the carbonization treatment following infusibility is performed in an inert gas atmosphere. Despite this, the strength decreases due to the influence of trace amounts of oxygen contained in the fiber bundle.
本発明者らは、かかる欠点を改良するために鋭
意検討した結果、酸化処理されたピツチから得ら
れる繊維を環元性液体中を通過させるか、およ
び/または100PPM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
100PPM未満である不活性気体中で炭化処理する
ことによつて強度が低下しない炭素繊維を得て、
本発明に到つた。 As a result of intensive studies to improve these drawbacks, the present inventors decided to pass the fibers obtained from oxidized pitch through a cyclic liquid and/or to pass an inert gas containing less than 100 PPM of oxygen. The oxygen content is then
Obtaining carbon fibers whose strength does not decrease by carbonization treatment in an inert gas having a concentration of less than 100 PPM,
We have arrived at the present invention.
即ち、本発明は、テトラヒドロキノリンで環元
処理されたピツ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
100PPM未満となるように該繊維を処理し、次い
で酸素含有量が100PPM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
とするピツチ類による炭素系繊維の製造方法提供
する。 That is, the present invention oxidizes fibers obtained from pitches treated with tetrahydroquinoline and then reduces the free oxygen content of the oxidized fibers.
Provided is a method for producing carbon fibers using pits, which comprises treating the fibers so that the oxygen content is less than 100 PPM, followed by carbonization in an inert gas having an oxygen content of less than 100 PPM, and graphitization if necessary. do.
本発明に用いられるピツチ類は例えば石油ピツ
チ、石炭タールピツチ、天然アスフアルト、工業
生産に際して副生されるピツチ状物等であり、テ
トラヒドロキノリンで環元処理される。ピツチ類
を環元処理するのに用いられるテトラヒドロキノ
リンはピツ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環元ピツチは例えば軟化点60
〜150℃のコールタールピツチとテトラヒドロキ
ノリンとを等重量含有し、溶解して、不溶分を濾
化したのち、350〜530℃で熱処理され、次に脱テ
トラヒドロキノリンを行い、400〜530℃で減圧下
熱処理して、軟化点200〜320℃に調製される。こ
のピツチは軟化点より20〜50℃高い温度に加熱し
て、ノズル径0.5〜0.15mm、紡糸速度200〜
1000m/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 include, for example, petroleum pitch, coal tar pitch, natural asphalt, and pitch-like substances produced as by-products during industrial production, and are subjected to ring treatment with tetrahydroquinoline. Tetrahydroquinoline, which is used for the ring treatment of pitches, also acts as a solvent for pitches. This tetrahydroquinoline ring element pitch has a softening point of 60, for example.
Coal tar pitch at ~150°C and tetrahydroquinoline are contained in equal weights, dissolved, and the insoluble matter is filtered, followed by heat treatment at 350~530°C, followed by removal of tetrahydroquinoline, and then at 400~530°C. Heat treated under reduced pressure to adjust the softening point to 200-320°C. This pitch is heated to a temperature 20~50℃ higher than the softening point, with a nozzle diameter of 0.5~0.15mm, and a spinning speed of 200~200mm.
Spinning at 1000 m/min yields 50-15 micron fibers. This fiber is oxidized in air at a temperature approximately 50°C below its softening point, e.g. 260°C, approximately 15°C.
The surface is oxidized and becomes infusible in a short period of ~60 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、炭化時の温度上昇を緩やか
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 treatment, and is inefficient because it is necessary to slow down the temperature rise during carbonization.
そこで、本発明は、かかる酸化処理された繊維
を環元性液体中を通過させるか、酸素含有量が
100PPM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つて該繊維中に含有され
る遊離の酸素量を100PPM以下にする。 Therefore, the present invention aims at passing such oxidized fibers through a cyclic liquid or reducing the oxygen content.
The amount of free oxygen contained in the fiber is reduced to 100 PPM or less by passing it through an inert gas of 100 PPM or less, or by treating it under reduced pressure.
酸化処理繊維中の遊離酸素を100PPMにするの
に用い得る環元性液体としては、チオ硫酸、亜硫
酸、スルフイン酸、スルフエン酸;カテコール、
ヒドロキノン、レゾルシンなどの芳香族に2ケ以
上の水酸基をもつ化合物などが挙げられる。この
環元性液体はアルカリによりPHを9以上に調節し
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。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
する方法が行われる。尚、上記環元性液体での処
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100PPM未満に調節するのによ
り効果的である。 Examples of cyclic liquids that can be used to reduce the free oxygen content in oxidized fibers to 100 PPM include thiosulfate, sulfite, sulfinic acid, sulfenic acid; catechol,
Examples include compounds having two or more hydroxyl groups on an aromatic group such as hydroquinone and resorcinol. This cyclic liquid is preferably one whose pH is adjusted to 9 or more with an alkali, and may be diluted with alcohol, acetone, or the like. An easy method for reducing the amount of oxygen in the fibers is to place the fibers that have been oxidized in an inert gas such as nitrogen or argon into a container and carry out displacement under reduced pressure. Incidentally, after the treatment with the above-mentioned cyclic liquid, performing a vacuum displacement treatment with an inert gas is more effective in controlling the free oxygen in the fibers to less than 100 PPM.
以上のようにして処理された繊維を100PPM以
上の酸素雰囲気にさらすことなく、100PPM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。 Without exposing the fibers treated as above to an oxygen atmosphere of 100 PPM or more, an oxygen-containing inert gas of less than 100 PPM, such as nitrogen, helium, etc.
Carbonized in argon and graphitized if necessary.
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 at approximately 800 to 1500°C in a metal furnace or refractory brick furnace under an inert gas atmosphere.
It is carried out under conditions of 5 to 60 minutes. Furthermore, if necessary, graphitization is usually performed in a graphite furnace under an atmosphere of argon or helium at about 1500 to 3000°C for 5 to 50 minutes.
It is carried out under the conditions of 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
量部をあらわす。 The carbon fiber obtained by the method of the present invention has excellent physical properties such as strength and elastic modulus. below,
The invention will be further illustrated by examples. In addition, parts represent parts by weight.
実施例 1
テトラヒドロキノリンで環元処理した軟化点
290℃のピツチより紡糸した18ミクロンの繊維を
空気中で260℃、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部よりなる環
元性液体に15分間浸漬し、水洗した。尚、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10mmHgに減圧した。こ
の繊維の酸素含有量は20PPMであつた。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
295Kg/mm2、弾性率は26t/mm2であつた。Example 1 Softening point after ring treatment with tetrahydroquinoline
18 micron fibers spun from pitch at 290°C were oxidized in air at 260°C for 20 minutes. This fiber was mixed with 12 parts of sodium thiosulfate, 0.5 part of resorcinol,
It was immersed in a cyclic liquid consisting of 100 parts of water and 5 parts of sodium hydroxide for 15 minutes, and then washed with water. Note that this immersion bath was replaced with nitrogen gas containing 50 PPM of oxygen. After washing with water, the fibers were vacuumed to 10 mmHg. The oxygen content of this fiber was 20 PPM. Next, it was dried in a 220° C. furnace purged with nitrogen gas, and heated in the same furnace at a rate of 50° C./min to 1500° C. for 30 minutes to obtain carbon fibers. The strength of this carbon fiber is
295Kg/mm 2 , and the elastic modulus was 26t/mm 2 .
尚、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℃まで昇温して30分加熱して得た炭素繊維の
強度は155Kg/mm2、弾性率は12t/mm2であつた。 For comparison, immediately after oxidation treatment, the test was carried out at 50℃/min in a nitrogen gas atmosphere containing 150PPM oxygen.
The carbon fiber obtained by heating it to 1500°C for 30 minutes had a strength of 155 Kg/mm 2 and an elastic modulus of 12 t/mm 2 .
実施例 2
テトラヒドロキノリンで環元処理した軟化点
250℃のピツチより紡糸した21ミクロン糸を用
い、環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/
mm2、弾性率12t/mm2であつた。Example 2 Softening point after ring treatment with tetrahydroquinoline
Using 21 micron thread spun from pitch at 250℃, 3 parts of hydroquinone and water are used as the cyclic liquid.
Carbon fibers were obtained in the same manner as in Example 1 except that a 100 parts dipping bath was used. The strength of this fiber is 208Kg/
mm 2 and elastic modulus of 12t/mm 2 .
尚、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168Kg/mm2、弾性率9.8t/mm2であつた。 For comparison, a carbon fiber carbonized in nitrogen gas containing 150 PPM of oxygen immediately after the oxidation treatment had a strength of 168 Kg/mm 2 and an elastic modulus of 9.8 t/mm 2 .
Claims (1)
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100PPM未満となるよ
うに該繊維を処理し、次いで酸素含有量が
100PPM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ツチ類
による炭素系繊維の製造方法。1. After oxidizing fibers obtained from pitches treated with tetrahydroquinoline, the fibers are treated so that the free oxygen content of the oxidized fibers is less than 100 PPM, and then the oxygen content is
A method for producing carbon-based fibers using pitches, characterized by carbonization treatment in an inert gas of less than 100 PPM, and graphitization treatment 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 JPS58144124A (en) | 1983-08-27 |
JPS6132406B2 true 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) |
Cited By (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 |
Cited By (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 |
Also Published As
Publication number | Publication date |
---|---|
JPS58144124A (en) | 1983-08-27 |
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