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JPS633972B2 - - Google Patents
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JPS633972B2 - - Google Patents

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Publication number
JPS633972B2
JPS633972B2 JP56131856A JP13185681A JPS633972B2 JP S633972 B2 JPS633972 B2 JP S633972B2 JP 56131856 A JP56131856 A JP 56131856A JP 13185681 A JP13185681 A JP 13185681A JP S633972 B2 JPS633972 B2 JP S633972B2
Authority
JP
Japan
Prior art keywords
fiber bundle
fiber
fibers
acrylonitrile
flame
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
JP56131856A
Other languages
Japanese (ja)
Other versions
JPS5836216A (en
Inventor
Minoru Hirai
Kazuo Izumi
Kenji Shimazaki
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.)
Teijin Ltd
Original Assignee
Toho Rayon 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 Toho Rayon Co Ltd filed Critical Toho Rayon Co Ltd
Priority to JP56131856A priority Critical patent/JPS5836216A/en
Publication of JPS5836216A publication Critical patent/JPS5836216A/en
Publication of JPS633972B2 publication Critical patent/JPS633972B2/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、アクリロニトリル系繊維束(トウ)
を出発原料として、膠着のない高い強度と優れた
紡績性を有し、かつ高強度の炭素繊維や繊維状活
性炭を得るのに適した耐炎化繊維束(トウ)を製
造する方法に関するものである。 アクリロニトリル系繊維束(トウ)を出発原料
とし、これを酸化性雰囲気中200〜400℃にて酸化
処理して耐炎性を有する繊維とし、これを織物、
編物、不織布等として用い、あるいは繊維状活性
炭、炭素繊維等の中間原料として利用することは
知られている。 このような耐炎化繊維束を経済的に得る場合、
原料のアクリロニトリル系繊維は繊維束(トウ)
の状態にて酸化処理することが好ましい。しかし
アクリロニトリル系繊維をトウの状態で酸化処理
すると、アクリロニトリル系重合体の特徴とし
て、繊維表面より軟化を生じ繊維相互間で表面が
膠着することがある。 更にアクリロニトリル系重合体は酸化処理時に
約50〜100Kcal/gの反応熱を発生し、この反応
熱が繊維束の内部に蓄熱し、繊維束内部の温度が
異常に高くなり繊維相互間の膠着による繊維束の
切断、剛直化等の現象が生じ、そのため操業の安
定性が損われ、繊維束の紡績性が低下し、更に繊
維状活性炭、炭素繊維とした場合の品質(紡績
性、強度、賦活収率、加工性)が低下し、品質斑
が発生する。 本発明者等はこうした問題につき検討の結果、 (1) アクリロニトリル系繊維束の酸化時における
膠着は酸化反応初期、特に酸素結合量8重量%
以下の段階において集中的に発生すること、 (2) 膠着はそれ以後の工程ではほとんど発生しな
いこと、 (3) この膠着は初期において容易に剥離(分離)
することができ、酸化処理が更に進んだ段階で
は分離が難しいことを見出した。 例えば45万デニールのアクリロニトリル系繊維
束(アクリロニトリル92%、アクリル酸メチル
4.5%、アクリルアミド3.5%、共重合体単繊維繊
度3デニールを245℃の空気中で酸化処理、酸素
結合量が2〜21重量%の範囲の各酸化処理繊維か
ら膠着発生率を求めた。 その結果を示すと第1図曲線Aの通りである。
このようにアクリロニトリル系繊維束を酸化処理
した場合、酸素結合量約8重量%までに殆んどの
膠着が発生し、それ以後では膠着の増加はない。 また、この膠着は初期の段階で強制的に開繊す
ると容易に分離できる。 かかる知見を基に本発明者等は検討の結果本発
明に至つた。 即ち、本発明は、アクリロニトリル系繊維束
(トウ)を酸化性雰囲気中で酸化処理し、耐炎化
繊維束を製造するに当り、酸素結合量4.5〜8重
量%まで酸化処理したときに、被処理繊維束を開
繊処理し、更に酸素結合量が15重量%以上になる
まで酸化処理を続けることを特徴とする耐炎化繊
維束の製造方法である。 かかる本発明によると、膠着のない高品質のア
クリロニトリル系耐炎化繊維束を得ることがき
る。ここで酸素結合量は柳本高速CHNコーダー
MT―2型によりC.H.Nを測定し次式によつて求
めたものである。 酸素結合量(%)= 試料重量−灰分−(CHN)合計量/試料重量−灰分×100
(%) また繊維束の膠着発生率は倍率500倍の繊維の
断面写真観察により次式にて求める。 膠着発生率(%) =膠着本数/写真中の繊維本数×100(%) 本発明においてアクリロニトリル系繊維束とは
アクリロニトリルを主体とする重合体からなる繊
維であり、通常アクリロニトリルを少くとも75重
量%以上含む共重合体又は重合体からなる繊維
で、コモノマーとしてはアクリル酸、メタクリル
酸、アクリル酸メチル等の酸及びその誘導体等ア
クリロニトリルと共重合可能な不飽和化合物が用
いられる。 またこれらの重合体又は共重合体は他のアクリ
ロニトリル系共重合体又は重合体を混合して作ら
れた繊維も使用される。コモノマー量が25重量%
以上になると酸化処理時に表面の軟化状態が著し
く、膠着を生じ易くなり、また膠着繊維の分離も
悪くなる。 アクリロニトリル系繊維束としてはトータルデ
ニールは60000〜1700000デニール位のものが用い
られるが、通常は140000〜600000デニールで単繊
維は0.5〜15デニールのものが用いられる。 このようなアクリロニトリル系の繊維束の酸化
処理は酸化雰囲気例えば空気中において200〜400
℃にて行なわれる。処理中の張力は、炭素繊維製
造用の耐炎化繊維束を製造する場合には、その処
理温度での繊維の自由収縮率の40〜60%であり、
活性炭用の場合は50〜90%の収縮状態にて行な
う。また繊維束の密度は処理温度によつても異な
るが、600g/m2以下好ましくは200〜400g/m2
の範囲である。 酸化処理は酸素結合量が15重量%以上になるま
で行なわれるが、酸素結合量が4.5〜8重量%ま
で進んだ状態の繊維束に対して開繊処理を行な
う。ここでの開繊処理とは繊維束をさばいて繊維
相互の膠着を分離し、膠着繊維を分離させ、単繊
維とすることを意味し、その手段としては種々の
方法が考えられる。 例えば繊維束を空気中、水中で高い振動を与え
ること、折りたたむこと、更にローラ、固定ピ
ン、バーなどで“しごく”方法などがある。特に
好ましい方法は繊維束を屈曲させるとともに擦過
させる方法である。 第2図において1は固定子、2は繊維束を示
す。繊維束の屈曲角度αは25〜60度が好ましく特
に好ましくは35〜45度である。 角度が25度より小さいと繊維束が低伸度のため
に、繊維の劣化を招いたり、切断されたりする。
また60度以上の場合は開繊効果が低い。具体的な
方法としては第3図に示すようなものがある。開
繊処理を行う場合、酸素結合量が4.5〜8重量%
の時に行なうのがよい。 開繊処理を酸素結合量4.5重量%以前の段階で
行なうと、その後再び酸化工程で再膠着を生じ、
開繊処理の効果が消滅する一方、8重量%以上に
まで酸化が進んだときに処理を行なうと繊維の強
伸度が低下しているために、繊維の折れや切断を
生じる。かつ膠着の分離も難しい。 最も好ましくは5〜7重量%の酸素結合量のと
きに開繊処理を行うことである。 開繊処理の温度は開繊処理前の温度より80℃〜
200℃ほど低い温度で行なうのが良い。 80℃以下の低い温度で行なうと、繊維の圧着に
より膠着を増し、200℃以上低温度で処理すると
膠着が取れ難い。 更に、この開繊処理前に鉄化合物、チタン化合
物、アルミニウム化合物、硅素化合物及び炭素粉
末等を繊維に添着または含有させた後開繊処理す
ると、更に効果は倍増する。このように酸化工程
の中間に開繊処理を行うと膠着発生率が著しく減
少する。 例えばアクリロニトリル90%、アクリルアミド
10%のアクリロニトリル系繊維よりなる150万デ
ニール(単繊維繊度2デニール)を260℃の空気
中で酸化処理し、該繊維の酸素結合量が下記の段
階において第3図イの装置にて屈曲角度50度、温
度は酸化温度より180℃低い80℃にて連続的に4
回の屈曲処理を行い、更に270℃にて酸化処理し、
酸素結合量20%になつた耐炎化繊維の膠着発生
率、繊維強度、紡績性(リアクターテスト)につ
いて括めると第1表のようになつた。
The present invention relates to an acrylonitrile fiber bundle (tow)
This invention relates to a method for producing a flame-resistant fiber bundle (tow) using as a starting material, which has high strength without sticking, excellent spinnability, and is suitable for obtaining high-strength carbon fibers and fibrous activated carbon. . Starting material is acrylonitrile fiber bundle (tow), which is oxidized at 200 to 400°C in an oxidizing atmosphere to produce flame-resistant fibers, which can be used as textiles,
It is known to be used as knitted fabrics, nonwoven fabrics, etc., or as intermediate raw materials for fibrous activated carbon, carbon fibers, etc. When obtaining such flame-resistant fiber bundles economically,
The raw material acrylonitrile fiber is a fiber bundle (tow)
It is preferable to carry out the oxidation treatment under these conditions. However, when acrylonitrile fibers are oxidized in the form of tow, a characteristic of acrylonitrile polymers is that the fiber surfaces may become softer and the surfaces of the fibers may stick together. Furthermore, acrylonitrile-based polymers generate approximately 50 to 100 Kcal/g of reaction heat during oxidation treatment, and this reaction heat accumulates inside the fiber bundle, causing the temperature inside the fiber bundle to become abnormally high and causing fibers to stick together. Phenomena such as cutting and stiffening of the fiber bundle occur, which impairs the stability of operation, reduces the spinnability of the fiber bundle, and further reduces the quality (spinnability, strength, activation) of fibrous activated carbon and carbon fiber. (yield, processability) decreases, and quality irregularities occur. As a result of studies on these problems, the present inventors found that (1) stiction during oxidation of acrylonitrile fiber bundles occurs at the early stage of the oxidation reaction, especially when the amount of oxygen bonded is 8% by weight.
(2) Adhesion rarely occurs in the following steps; (3) Adhesion easily peels off (separates) in the initial stage;
It has been found that separation is difficult at an advanced stage of oxidation treatment. For example, a 450,000 denier acrylonitrile fiber bundle (92% acrylonitrile, methyl acrylate)
4.5% acrylamide, 3.5% acrylamide, copolymer single fiber fineness 3 denier was oxidized in air at 245°C, and the sticking occurrence rate was determined from each oxidized fiber with an oxygen bond amount in the range of 2 to 21% by weight. The results are shown in curve A in Figure 1.
When an acrylonitrile fiber bundle is oxidized in this way, most of the adhesion occurs up to about 8% by weight of oxygen bonding, and there is no increase in adhesion after that point. Moreover, this sticking can be easily separated by forcibly opening the fibers at an early stage. Based on this knowledge, the present inventors conducted studies and arrived at the present invention. That is, in the present invention, when an acrylonitrile fiber bundle (tow) is oxidized in an oxidizing atmosphere to produce a flame-resistant fiber bundle, when the oxidation treatment is applied to an oxygen bond amount of 4.5 to 8% by weight, This is a method for producing a flame-resistant fiber bundle, which comprises opening the fiber bundle and continuing the oxidation treatment until the amount of oxygen bonded becomes 15% by weight or more. According to the present invention, it is possible to obtain a high quality acrylonitrile-based flame-resistant fiber bundle that is free from sticking. Here, the amount of oxygen bond is determined by Yanagimoto high-speed CHN coder.
CHN was measured using Model MT-2 and calculated using the following formula. Oxygen binding amount (%) = Sample weight - Ash content - (CHN) total amount / Sample weight - Ash content x 100
(%) In addition, the incidence of sticking of fiber bundles is determined by the following formula by observing cross-sectional photographs of fibers at 500x magnification. Incidence of sticking (%) = Number of stuck fibers / Number of fibers in the photo × 100 (%) In the present invention, an acrylonitrile fiber bundle is a fiber made of a polymer mainly composed of acrylonitrile, and usually contains at least 75% by weight of acrylonitrile. In fibers made of copolymers or polymers containing the above, unsaturated compounds copolymerizable with acrylonitrile, such as acids such as acrylic acid, methacrylic acid, and methyl acrylate, and derivatives thereof, are used as comonomers. Fibers made by mixing these polymers or copolymers with other acrylonitrile copolymers or polymers may also be used. Comonomer content is 25% by weight
If the temperature exceeds that level, the surface will be significantly softened during the oxidation treatment, and sticking will occur easily, and separation of stuck fibers will also become difficult. The acrylonitrile fiber bundle used has a total denier of about 60,000 to 1,700,000 deniers, but usually has a total denier of 140,000 to 600,000 deniers, and single fibers of 0.5 to 15 deniers are used. Such oxidation treatment of acrylonitrile-based fiber bundles is carried out in an oxidizing atmosphere, for example, in air at a temperature of 200 to 400
It is carried out at ℃. The tension during processing is 40 to 60% of the free shrinkage rate of the fiber at the processing temperature when producing flame-resistant fiber bundles for carbon fiber production.
In the case of activated carbon, it is performed in a 50 to 90% contracted state. The density of the fiber bundle also varies depending on the processing temperature, but is less than 600 g/ m2 , preferably 200 to 400 g/ m2.
is within the range of The oxidation treatment is carried out until the amount of oxygen binding reaches 15% by weight or more, and the fiber bundle in which the amount of oxygen binding has reached 4.5 to 8% by weight is subjected to the opening treatment. The opening treatment here means opening the fiber bundle to separate the fibers from sticking together, separating the stuck fibers, and making them into single fibers, and various methods can be considered as means for this purpose. For example, methods include applying high vibrations to fiber bundles in air or water, folding them, and ``squeezing'' them with rollers, fixing pins, bars, etc. A particularly preferred method is a method in which the fiber bundle is bent and rubbed. In FIG. 2, 1 indicates a stator and 2 indicates a fiber bundle. The bending angle α of the fiber bundle is preferably 25 to 60 degrees, particularly preferably 35 to 45 degrees. If the angle is smaller than 25 degrees, the fiber bundle will have low elongation, leading to fiber deterioration or breakage.
Furthermore, if the temperature is 60 degrees or higher, the opening effect will be low. A specific method is as shown in FIG. When performing fiber opening treatment, the amount of oxygen binding is 4.5 to 8% by weight.
It is best to do it when If opening treatment is performed before the amount of oxygen binding is 4.5% by weight, re-agglutination will occur in the subsequent oxidation process.
While the effect of the opening process disappears, if the process is performed when oxidation has progressed to 8% by weight or more, the strength and elongation of the fibers has decreased, resulting in folding or cutting of the fibers. It is also difficult to separate the stalemates. Most preferably, the opening treatment is performed when the amount of oxygen bonding is 5 to 7% by weight. The temperature of the opening process is 80°C or more than the temperature before the opening process.
It is best to do this at a temperature as low as 200℃. If the process is carried out at a low temperature below 80°C, the fibers will be compressed, resulting in increased adhesion, and if the process is carried out at a low temperature above 200°C, the adhesion will be difficult to remove. Furthermore, if an iron compound, a titanium compound, an aluminum compound, a silicon compound, a carbon powder, etc. are attached to or contained in the fibers before the opening treatment, and then the opening treatment is performed, the effect is further doubled. When the fiber opening treatment is performed in the middle of the oxidation process as described above, the incidence of sticking occurs is significantly reduced. For example, acrylonitrile 90%, acrylamide
A 1.5 million denier (single fiber fineness 2 denier) made of 10% acrylonitrile fiber is oxidized in air at 260°C, and the amount of oxygen bonded in the fiber is determined by the bending angle using the apparatus shown in Figure 3 A at the following stages. 50 degrees, and the temperature is 80 degrees Celsius, which is 180 degrees lower than the oxidation temperature.
After bending twice and then oxidizing at 270℃,
Table 1 summarizes the sticking occurrence rate, fiber strength, and spinnability (reactor test) of flame-resistant fibers with an oxygen binding content of 20%.

【表】 また屈曲角度の影響を調べるため、アクリロニ
トリル90%、塩化ビニリデン10%からなる組成を
有するアクリロニトリル系繊維よりなる90000デ
ニール(単繊維繊度3デニール)を250℃の空気
中で酸化処理し、該繊維の酸素結合量が6%の段
階において、第3図イの装置にて種々の屈曲角度
で酸化温度より190℃低い60℃の温度のもとで連
続的に7回の屈曲処理を行い、更に270℃にて酸
化処理し、酸素結合量が19.5%の耐炎化繊維を作
成し、この耐炎化繊維の酸化工程の後半の安定性
と、該耐炎化繊維の膠着発生率及び繊維強度につ
いて第2表に括めた。
[Table] In order to investigate the effect of bending angle, 90,000 denier (single fiber fineness 3 denier) made of acrylonitrile fiber with a composition of 90% acrylonitrile and 10% vinylidene chloride was oxidized in air at 250°C. When the amount of oxygen binding in the fiber was 6%, the fiber was continuously bent seven times at various bending angles at a temperature of 60°C, which is 190°C lower than the oxidation temperature, using the apparatus shown in Figure 3A. , and further oxidized at 270℃ to create a flame-resistant fiber with an oxygen bonding amount of 19.5%.The stability of this flame-resistant fiber in the latter half of the oxidation process, the occurrence rate of adhesion, and the fiber strength of the flame-resistant fiber were investigated. It is summarized in Table 2.

【表】【table】

【表】 次に第2表で得たNo.1,No.5の耐炎化繊維を
1000℃にて水蒸気中にて賦活し、比表面積1000
m2/gの繊維状活性炭を得た。 これらの活性炭の賦活収率、繊維強度は以下の
通りである。
[Table] Next, the No. 1 and No. 5 flame-resistant fibers obtained in Table 2 are
Activated in steam at 1000℃, specific surface area 1000
Fibrous activated carbon of m 2 /g was obtained. The activation yield and fiber strength of these activated carbons are as follows.

【表】 以上の如く、本発明により繊維の膠着は減少し
耐炎化工程で繊維から発生する熱は蓄熱すること
なく周囲に拡散して、生産効率も向上できた。一
方製造される耐炎化繊維も膠着が少ないため紡績
性も優れ、繊維状活性炭の原料としても賦活収率
が優れ、かつ繊維強度の高いものが得られ、また
炭素繊維の原料としても高強力なものが製造でき
る。 以下本発明の実施例について説明する。 実施例 1 アクリロニトリル94%、アクリル酸メチル6%
の共重合組成の繊維からなる45万デニールのアク
リロニトリル系繊維束(単繊維繊度3デニール)
を250℃の空気中にて酸素結合量が6.5%まで酸化
し、第3図イの装置にて85℃で開繊処理し、更に
270℃にて処理し、酸素結合量が19.5%まで酸化
した。この耐炎化繊維束の繊維強度は26.5Kg/mm2
で、この繊維の膠着発生率は2.4%であつた。 この繊維束を用い水蒸気中にて900℃で賦活処
理し、比表面積1050m2/gの繊維状活性炭を作つ
た。得られた活性炭の賦活収率は25%、繊維強度
は40Kg/mm2であつた。 比較例 実施例1において開繊処理しないで、同一処理
条件で酸化処理したところ、繊維の膠着が多発
し、膠着部が切断し、満足な耐炎化繊維を得るこ
とができなかつた。そのため酸化温度を緩和し、
260℃にて酸素結合量19.5%まで酸化した。 得られた耐炎化繊維の繊維強度は21Kg/mm2であ
り、膠着発生率は17.5%であつた。得られた繊維
を水蒸気中にて900℃で賦活処理し、比表面積
1000m2/gの繊維状活性炭を得た。この時の賦活
収率は20%で繊維状活性炭の強度は20Kg/mm2であ
つた。
[Table] As described above, according to the present invention, the sticking of fibers was reduced, the heat generated from the fibers during the flameproofing process was diffused to the surroundings without being stored, and production efficiency was also improved. On the other hand, the flame-retardant fibers produced also have excellent spinnability due to their low adhesion, and can be used as raw materials for fibrous activated carbon with excellent activation yields and high fiber strength.They can also be used as raw materials for carbon fibers with high strength. Things can be manufactured. Examples of the present invention will be described below. Example 1 Acrylonitrile 94%, methyl acrylate 6%
450,000 denier acrylonitrile fiber bundle (single fiber fineness 3 denier) consisting of fibers with a copolymer composition of
was oxidized in air at 250℃ until the amount of oxygen bonded was 6.5%, opened at 85℃ using the equipment shown in Figure 3A, and further
It was treated at 270°C, and the amount of oxygen bonded was oxidized to 19.5%. The fiber strength of this flame-resistant fiber bundle is 26.5Kg/mm 2
The incidence of sticking of this fiber was 2.4%. This fiber bundle was activated at 900° C. in steam to produce fibrous activated carbon with a specific surface area of 1050 m 2 /g. The activated carbon obtained had an activation yield of 25% and a fiber strength of 40 kg/mm 2 . Comparative Example When the fibers of Example 1 were subjected to oxidation treatment under the same treatment conditions without being subjected to the opening treatment, the fibers frequently stuck together, the stuck portions were cut, and a satisfactory flame-resistant fiber could not be obtained. Therefore, the oxidation temperature is relaxed,
It was oxidized at 260°C to an oxygen bond amount of 19.5%. The obtained flame-resistant fiber had a fiber strength of 21 Kg/mm 2 and a sticking occurrence rate of 17.5%. The obtained fibers were activated at 900℃ in steam, and the specific surface area
1000 m 2 /g of fibrous activated carbon was obtained. The activation yield at this time was 20% and the strength of the fibrous activated carbon was 20 kg/mm 2 .

【図面の簡単な説明】[Brief explanation of the drawing]

第1図はトウを酸化処理した場合における酸化
処理の進行に伴う膠着の発生状況を示したもので
ある。第2図は、本発明屈曲処理の角度を示す説
明図である。第3図は、本発明屈曲処理の態様を
示す概略図であり、イは固定バーによる屈曲擦過
処理、ロは組合せられた歯車による処理、ハはク
リンパーによる屈曲処理を夫々示したものであ
る。
FIG. 1 shows the occurrence of sticking as the oxidation treatment progresses when tow is oxidized. FIG. 2 is an explanatory diagram showing the angle of the bending process of the present invention. FIG. 3 is a schematic view showing an embodiment of the bending process of the present invention, in which A shows the bending and scratching process using a fixed bar, B shows the process using the combined gears, and C shows the bending process using the crimper.

Claims (1)

【特許請求の範囲】 1 アクリロニトリル系繊維束(トウ)を酸化性
雰囲気中で酸化処理し、耐炎化繊維束を製造する
に当り、酸素結合量4.5〜8重量%まで酸化処理
したときに、被処理繊維束を開繊処理し、更に酸
素結合量が15重量%以上になるまで酸化処理を続
けることを特徴とする耐炎化繊維束の製造方法。 2 開繊処理が、被処理繊維束を25〜60度の角度
で屈曲擦過を行うことである特許請求の範囲1の
方法。 3 開繊処理時の温度が、当該処理前の繊維束の
温度より80〜200℃ほど低温である特許請求の範
囲1の方法。
[Claims] 1. When an acrylonitrile fiber bundle (tow) is oxidized in an oxidizing atmosphere to produce a flame-resistant fiber bundle, when the oxidation treatment is performed to an oxygen bond content of 4.5 to 8% by weight, A method for producing a flame-resistant fiber bundle, which comprises opening the treated fiber bundle and continuing the oxidation treatment until the amount of oxygen binding reaches 15% by weight or more. 2. The method according to claim 1, wherein the opening treatment includes bending and rubbing the fiber bundle to be treated at an angle of 25 to 60 degrees. 3. The method according to claim 1, wherein the temperature during the opening treatment is about 80 to 200°C lower than the temperature of the fiber bundle before the treatment.
JP56131856A 1981-08-22 1981-08-22 Production of bundle of preoxidized fiber Granted JPS5836216A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56131856A JPS5836216A (en) 1981-08-22 1981-08-22 Production of bundle of preoxidized fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56131856A JPS5836216A (en) 1981-08-22 1981-08-22 Production of bundle of preoxidized fiber

Publications (2)

Publication Number Publication Date
JPS5836216A JPS5836216A (en) 1983-03-03
JPS633972B2 true JPS633972B2 (en) 1988-01-27

Family

ID=15067717

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56131856A Granted JPS5836216A (en) 1981-08-22 1981-08-22 Production of bundle of preoxidized fiber

Country Status (1)

Country Link
JP (1) JPS5836216A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58214525A (en) * 1982-06-07 1983-12-13 Toray Ind Inc Production of carbon fiber
US4588538A (en) * 1984-03-15 1986-05-13 Celanese Corporation Process for preparing tapes from thermoplastic polymers and carbon fibers
DE3569396D1 (en) * 1984-11-21 1989-05-18 Mitsubishi Chem Ind Method for fibrillating carbonaceous fibers
KR102586391B1 (en) 2018-01-26 2023-10-11 도레이 카부시키가이샤 Method for producing flame retardant fiber bundles and carbon fiber bundles
RU2020122407A (en) 2018-01-26 2022-02-28 Торэй Индастриз, Инк. STABILIZED FIBER BEAM AND METHOD FOR PRODUCING CARBON FIBER BEAM

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5221425A (en) * 1975-08-11 1977-02-18 Asahi Chem Ind Co Ltd Process for manufacturing carbon fibers
JPS52107328A (en) * 1976-03-03 1977-09-08 Toho Rayon Co Ltd Production of carbon fiber from acrylic fiber
JPS5853086B2 (en) * 1976-10-01 1983-11-26 東邦ベスロン株式会社 Method for producing flame-resistant fibers
JPS5352735A (en) * 1976-10-25 1978-05-13 Toho Rayon Co Ltd Production of pre-oxidized fiber

Also Published As

Publication number Publication date
JPS5836216A (en) 1983-03-03

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