JPH0376823A - Production of acrylonitrile polymer-based carbon fiber - Google Patents
Production of acrylonitrile polymer-based carbon fiberInfo
- Publication number
- JPH0376823A JPH0376823A JP12545990A JP12545990A JPH0376823A JP H0376823 A JPH0376823 A JP H0376823A JP 12545990 A JP12545990 A JP 12545990A JP 12545990 A JP12545990 A JP 12545990A JP H0376823 A JPH0376823 A JP H0376823A
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- Japan
- Prior art keywords
- polymer
- acrylonitrile
- acrylonitrile polymer
- strength
- carbon fiber
- 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.)
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- Inorganic Fibers (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、高立体規則性アクリロニトリル重合体から焼
成速度が速く、高強度、高弾性率を有する炭素繊維の製
法に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for producing carbon fibers having a high firing rate, high strength, and high modulus of elasticity from a highly stereoregular acrylonitrile polymer.
炭素繊維分野では、従来より、出発原料の重合体におけ
る共重合成分の検討、耐炎化段階での延伸、炭化工程で
の温度コントロール、又、プロセス内の不純物や不要残
存物等を減少させる等の方法で、炭素繊維の強度、弾性
率を上げる研究がなされてきた。又、焼成速度を速める
ためにカルボン酸等を含むモノマーを共重合させる方法
等が用いられてきた。In the field of carbon fibers, there have been many efforts such as examining copolymerization components in the starting material polymer, stretching during the flameproofing stage, temperature control during the carbonization process, and reducing impurities and unnecessary residues in the process. Research has been conducted to increase the strength and elastic modulus of carbon fibers. Additionally, in order to increase the firing rate, methods have been used in which monomers containing carboxylic acids and the like are copolymerized.
しかしながら、黒鉛結晶の理論強度が18000kg/
−1理論弾性率が1007on/−であるのに対して、
アクリロニトリル重合体系炭素繊維では、高強度炭素繊
維と呼ばれるもので強度が250〜700kg/d(理
論強度の1.4〜3.9%)、弾性率が20〜30To
n/d、高弾性率炭素繊維と呼ばれるもので強度が25
0〜350 kg/ij、弾性率が35〜45 Ton
/−(理論弾性率の35〜45%)と強度、弾性率共に
理論値に程遠く、しかもピッチ系炭素繊維(強度: 1
50〜300 kg/lj、弾性率: 30〜70 T
on / d )に比べても強度は高いが、弾性率が低
い等の問題点がある。従って、産業資材、宇宙工学分野
等においても充分満足できる程の強度、弾性率を同時に
保持したものは得られておらず、アクリロニトリル重合
体系炭素繊維の用途展開が制限されているのが現状であ
る。However, the theoretical strength of graphite crystal is 18,000 kg/
-1 theoretical elastic modulus is 1007on/-,
Acrylonitrile polymer carbon fibers are called high-strength carbon fibers and have a strength of 250 to 700 kg/d (1.4 to 3.9% of theoretical strength) and an elastic modulus of 20 to 30 To.
n/d, which is called high modulus carbon fiber and has a strength of 25
0~350 kg/ij, elastic modulus 35~45 Ton
/- (35 to 45% of the theoretical elastic modulus), which is far from the theoretical value for both strength and elastic modulus, and moreover, pitch-based carbon fiber (strength: 1
50-300 kg/lj, elastic modulus: 30-70 T
Although the strength is higher than that of on/d), there are problems such as a low elastic modulus. Therefore, it has not been possible to obtain a fiber that simultaneously maintains sufficient strength and elastic modulus in the fields of industrial materials, space engineering, etc., and the use of acrylonitrile polymer carbon fiber is currently limited. .
本発明者等は、かかる現状に鑑み、鋭意研究を重ねた結
果、立体規則性を高めたアクリロニトリル重合体を出発
原料とすることによって、炭素繊維の強度、弾性率を今
まで以上に向上させ、しかも同時に製造段階における焼
成速度を従来以上に速めることに成功した。In view of the current situation, the present inventors have conducted extensive research, and as a result, by using an acrylonitrile polymer with enhanced stereoregularity as a starting material, the strength and elastic modulus of carbon fibers have been improved more than ever before. Moreover, at the same time, they succeeded in increasing the firing speed during the manufacturing stage more than ever before.
即ち、本発明は、13C−NMRによって規定されるア
クリロニトリルモノマー連鎖部分のアイソタクチック・
トリアッド分率が少なくとも0.35である立体規則性
アクリロニトリル重合体からなる繊維を原料とすること
を特徴とする炭素繊維の製法である。That is, the present invention provides isotactic analysis of acrylonitrile monomer chain portions defined by 13C-NMR.
This is a method for producing carbon fibers, characterized in that fibers made of a stereoregular acrylonitrile polymer having a triad fraction of at least 0.35 are used as raw materials.
アイソタクチック・トリアッド分率とは、いわゆる立体
規則性表示法のうちのトリアット分率の1つであって、
アクリロニトリル重合体の場合には、例えば重水素化ジ
メチルスルフオキシド中に溶解した溶液の”C−NMR
のシアノ基の炭素のピーク強度から算定される。さらに
具体的にはポリマー・ジャーナル17巻1291頁(1
985)に記載されている上山らの方法で帰属したペン
タッド・タクチシティーに基づくピーク同定によって求
められる。即ち、”C−NMRの核磁気共鳴吸収の立体
規則性に基づくピーク分裂チャートにおいてシアノ基炭
素領域の全ピーク強度に対するmlnllJff1ml
llr+rmmrの3つのピークの強度の合計の割合が
アイソタクチック・トリアッド分率である。Isotactic triad fraction is one of the triat fractions in the so-called stereoregularity representation method,
In the case of acrylonitrile polymers, for example, "C-NMR" of solutions dissolved in deuterated dimethyl sulfoxide
It is calculated from the peak intensity of the carbon of the cyano group. More specifically, Polymer Journal Vol. 17, p. 1291 (1
It is determined by peak identification based on pentad tacticity assigned by the method of Ueyama et al. described in 985). That is, "mlnllJff1ml for the total peak intensity of the cyano group carbon region in the peak splitting chart based on the stereoregularity of nuclear magnetic resonance absorption of C-NMR.
The ratio of the sum of the intensities of the three peaks llr+rmmr is the isotactic triad fraction.
この測定に際しては、分解能を上げ定量性をもたせるた
めにとくにシアノ基中炭素の吸収ピーク95域(119
〜121 ppcテトラメチルシラン基準)のみに着目
し、そのピークを中心に±500Hzを観測する。装置
としては日本電子製フーリエ変換NMR(FX−200
”)を使用し、溶媒としては重水素化ジメチルスルフオ
キシドを用い、試料濃度を3〜20重量%に調整する。In this measurement, in order to increase the resolution and provide quantitative performance, we particularly focused on the absorption peak in the 95 region (119
~121 ppc (based on tetramethylsilane) only, and observe ±500 Hz around that peak. The equipment is a Fourier transform NMR manufactured by JEOL (FX-200).
”), deuterated dimethyl sulfoxide is used as the solvent, and the sample concentration is adjusted to 3 to 20% by weight.
測定条件としては、温度80°C1観測周波数幅100
0 Hz、データ・ポイント16に、 lH’を時間6
.5μs (45’パルス)パルス遅延時間2.5 s
、サンプリング時間8.1s、積算回数64 X 1
0〜64 X 100に設定する。The measurement conditions are: temperature 80°C, observation frequency width 100°C.
0 Hz, data point 16, lH' at time 6
.. 5μs (45' pulse) Pulse delay time 2.5s
, sampling time 8.1s, integration number 64 x 1
Set to 0~64 x 100.
本発明の目的を達する炭素繊維を得るために使用される
立体規則性アクリロニトリル重合体のアイソタクチック
・トリアッド分率は、0.35以上が必要である。この
値よりも小さいと焼成速度が、従来の出発原料に共重合
体を含んだものより低下し、生産性が悪い。同時に、充
分満足のゆく強度や弾性率が得られない。特に、高弾性
率の発現にはアイツタクチイック・トリアット分率が0
.35以上であることが必要である。The isotactic triad fraction of the stereoregular acrylonitrile polymer used to obtain carbon fibers that achieve the purpose of the present invention must be 0.35 or more. If the value is smaller than this, the firing rate will be lower than that of conventional starting materials containing a copolymer, resulting in poor productivity. At the same time, sufficiently satisfactory strength and elastic modulus cannot be obtained. In particular, for the development of high elastic modulus, the tactical triat fraction is 0.
.. It must be 35 or more.
本発明中におけるアクリロニトリル重合体とは、少なく
とも90重量%のアクリロニトリルを含有する重合体を
いう。共重合成分を含有することは何等差し支えないが
、単一重合体の方が効果が大きい。共重合成分としては
例えばアクリル酸メチルなどのアクリル酸アルキル、メ
タクリル酸メチルなどのメタクリル酸アルキル、メタク
リロニトリル、クロトンニトリルなどのアルキル置換ア
クリロニトリル、2−ビニルピリジンなどのアルキル置
換ビニルピリジンなどが挙げられる。The acrylonitrile polymer in the present invention refers to a polymer containing at least 90% by weight of acrylonitrile. There is no problem in containing a copolymer component, but a single polymer is more effective. Examples of copolymerization components include alkyl acrylates such as methyl acrylate, alkyl methacrylates such as methyl methacrylate, alkyl-substituted acrylonitriles such as methacrylonitrile and crotonitrile, and alkyl-substituted vinylpyridines such as 2-vinylpyridine. .
立体規則性アクリロニトリル重合体の代表的な製法例を
二種示す。一つは尿素/アクリロニトリルの包接化合物
にγ線などの活性線を照射するものであり〔例えば、特
願昭61−120242号〕、いま一つは有機金属化合
物を開始剤としてアニオン重合法により合成するもので
ある〔例えば、特願昭63−26522号〕、前者の合
成方法を詳細に述べると、まずアクリロニトリルに分子
量Wl fIff剤として例えばノルマルブチルメルカ
プタンをアクリロニトリルに対し0.002モル添加し
て、予めメタノール/水系で再結晶して精製した尿素と
をモル比で1:1.5の割合でジュワー瓶に入れ、混合
し密閉したものを、−78°Cにドライアイスを用いて
冷却しつつ約6日間静置する。次に、−78°Cで10
.000キユーリーのγ線を照射線量率1.6X10’
レントゲン/時間で約100分照射し、次いで、反応
物を温水およびメタノールで洗浄し、尿素を完全に除去
し精製する。Two typical examples of methods for producing stereoregular acrylonitrile polymers are shown below. One is to irradiate the urea/acrylonitrile clathrate compound with active rays such as gamma rays [for example, Japanese Patent Application No. 120242/1983], and the other is to irradiate the urea/acrylonitrile clathrate compound with active rays such as gamma rays [for example, Japanese Patent Application No. 120242/1983]. [For example, Japanese Patent Application No. 63-26522]. To describe the former synthesis method in detail, first, 0.002 mol of n-butyl mercaptan is added to acrylonitrile as a molecular weight Wl f If agent. , and urea purified by recrystallization in a methanol/water system in advance at a molar ratio of 1:1.5 were placed in a dewar bottle, mixed and sealed, and cooled to -78°C using dry ice. Let stand for about 6 days. Then, at −78 °C for 10
.. 000 curie gamma rays at a dose rate of 1.6X10'
After approximately 100 minutes of X-ray/hour irradiation, the reaction is washed with warm water and methanol to completely remove and purify the urea.
次に後者の有機金属化合物を用いる合成法について述べ
ると、蒸発成分を凝縮しそれを還流できるように組まれ
た静置において、まず三つロフラスコを窒素置換し、こ
れに例えば重合溶剤としてのキシレン(三種の異性体混
合物)を入れて温度を120°Cに調節したあと、重合
開始剤として例えばジノルマルヘキシルマグネシウムの
1.0モル濃度へブタン溶液を添加してIO分間放置す
る。次にアクリロニトリルを10cc滴下して60分重
合させる。Next, we will discuss the latter method of synthesis using organometallic compounds. First, a three-necked flask is purged with nitrogen in a stationary system designed to condense the evaporated components and reflux them. (a mixture of three isomers) and the temperature was adjusted to 120°C, and then a butane solution was added to a 1.0 molar concentration of di-n-hexylmagnesium as a polymerization initiator, and left for IO minutes. Next, 10 cc of acrylonitrile was added dropwise and polymerized for 60 minutes.
これに、適当量の塩酸メタノール混合溶液を加えて重合
反応を終了させ、以下濾過と水洗を繰り返して精製する
。このようにして得られた重合体を紡糸するにあたって
用いられる溶剤としてはプロトン酸もしくはその水溶液
、無機塩類水溶液、あるいは無機塩類を含有した有機溶
媒が好適である。An appropriate amount of a mixed solution of hydrochloric acid and methanol is added to this to terminate the polymerization reaction, followed by repeated filtration and water washing for purification. The solvent used for spinning the polymer thus obtained is preferably a protonic acid or an aqueous solution thereof, an aqueous solution of an inorganic salt, or an organic solvent containing an inorganic salt.
プロトン酸とは分子内に水素を有する酸のことを言う。A protonic acid is an acid that has hydrogen in its molecule.
プロトン酸の例としては、硝酸、硫酸、各種リン酸、弗
化水素酸、塩化水素酸、臭化水素酸、沃化水素酸、過塩
素酸等の無機酸をはじめとして、酢酸ジクロロ酢酸、ト
リクロロ酢酸、トリフルオロ酢酸等各種の有機酸が挙げ
られる。また、水、フェノール類、アルコール類もプロ
トン酸に含まれる。密閉系において、水の場合は摂氏1
80度を超える条件で、フェノール類、アルコール類も
各化合物に応じた温度以上の条件において立体規則性の
高いアクリロニトリル重合体を溶解せしめることができ
る。Examples of protonic acids include inorganic acids such as nitric acid, sulfuric acid, various phosphoric acids, hydrofluoric acid, hydrochloric acid, hydrobromic acid, hydroiodic acid, perchloric acid, acetic acid dichloroacetic acid, trichloroacetic acid, etc. Examples include various organic acids such as acetic acid and trifluoroacetic acid. Water, phenols, and alcohols are also included in protonic acids. 1 degree Celsius for water in a closed system
Acrylonitrile polymers with high stereoregularity can be dissolved under conditions of temperatures exceeding 80 degrees Celsius, phenols and alcohols as well as conditions higher than the temperature corresponding to each compound.
無機塩類水溶液も立体規則性の高いアクリロニトリル重
合体を溶解せしめる。そのように用いられる無機塩類の
例としてはロダン酸ナトリウム、ロダン酸リチウム、ロ
ダン酸カルシウム、ロダン酸亜鉛等の各種ロダン酸塩、
塩化亜鉛、弗化亜鉛を始めとする各種のハロゲン含有塩
類、過塩素酸ナトリウム、過塩素酸カルシウム、過塩素
酸バリウム、過塩素酸アルミニウム等の過塩素酸塩が挙
げられる。Aqueous solutions of inorganic salts also dissolve highly stereoregular acrylonitrile polymers. Examples of such inorganic salts include various rhodanates such as sodium rhodanate, lithium rhodanate, calcium rhodanate, zinc rhodanate,
Examples include various halogen-containing salts such as zinc chloride and zinc fluoride, and perchlorates such as sodium perchlorate, calcium perchlorate, barium perchlorate, and aluminum perchlorate.
また、無機塩類を含有した有機溶媒も用いられる。無機
塩類を添加しない有機溶剤は該重合体を全く溶解しない
かもしくは膨潤する程度できわめて溶解が困難である。Furthermore, organic solvents containing inorganic salts may also be used. Organic solvents to which no inorganic salts are added do not dissolve the polymer at all or only swell it, making it extremely difficult to dissolve the polymer.
これに相当する有機溶剤としては例として、ジメチルフ
ォルムアミド、ジメチルスルフオキシド、ジメチルアセ
トアミド、スクシノニトリル、γ−ブチロラクトン、エ
チレンカーボネート水溶液、ヒドロオキシアセトニトリ
ル等が挙げられる。添加する無機塩としては、塩化リチ
ウム、弗化リチウムなどが用いられる。Examples of corresponding organic solvents include dimethylformamide, dimethylsulfoxide, dimethylacetamide, succinonitrile, γ-butyrolactone, aqueous ethylene carbonate solution, and hydroxyacetonitrile. As the inorganic salt to be added, lithium chloride, lithium fluoride, etc. are used.
この重合体の紡糸法としては一般の乾式、湿式、乾湿式
紡糸が適用可能である。湿式もしくは乾湿式紡糸を行う
際に、凝固浴の臨界濃度より低い濃度の凝固浴濃度で紡
糸することももちろん可能であるが、さらに臨界濃度よ
り高い凝固浴濃度で紡糸することによってアクリロニト
リル重合体からなる繊維の焼成速度が一層速くなり結晶
性の高い炭素繊維が製造出来る。As a spinning method for this polymer, general dry spinning, wet spinning, and dry-wet spinning can be applied. When performing wet or dry-wet spinning, it is of course possible to spin at a coagulation bath concentration lower than the critical concentration of the coagulation bath, but it is also possible to spin the acrylonitrile polymer at a coagulation bath concentration higher than the critical concentration. The firing speed of the fiber becomes even faster, and carbon fiber with high crystallinity can be produced.
臨界濃度とは、最大紡糸速度が最小、或いは全く紡糸不
可能となり、その両側の濃度においては紡糸可能領域を
有する凝固浴中の溶剤濃度を意味する。By critical concentration is meant the concentration of solvent in the coagulation bath at which the maximum spinning speed is at a minimum or no spinning is possible, and on either side of which there is a region where spinning is possible.
さらに、延伸により、繊維の結晶配向性をよくすること
ができる。その延伸としては、例えばゲル延伸(溶剤残
存状態における延伸)、熱水中延伸、蒸気延伸、熱風延
伸、熱媒延伸(加熱された有機液体中での延伸)、乾熱
延伸(乾熱ロール等による延伸)などが挙げられる。こ
れらの延伸方法の複数個を組み合わせて用いることも可
能である。Furthermore, the crystal orientation of the fibers can be improved by stretching. Examples of such stretching include gel stretching (stretching in a state where a solvent remains), hot water stretching, steam stretching, hot air stretching, heating medium stretching (stretching in a heated organic liquid), and dry heat stretching (dry heat roll, etc.). stretching). It is also possible to use a combination of a plurality of these stretching methods.
アクリロニトリル重合体からなる繊維から炭素繊維を得
るには、このようにして紡糸された繊維を空気雰囲気中
200〜300°Cで、加熱することにより炭化指数(
以下C0■と略記する)が、0.50〜0.65の範囲
となる耐炎化繊維を得た後、窒素雰囲気中400〜20
00°Cの温度で炭化処理を行うことが好ましい。To obtain carbon fiber from fibers made of acrylonitrile polymer, the carbonization index (carbonization index) is
After obtaining flame-resistant fibers with a C0 (hereinafter abbreviated as C0■) in the range of 0.50 to 0.65,
It is preferable to carry out the carbonization treatment at a temperature of 00°C.
C,Iとはカーボニゼイション・インデックス(Car
bonization Index)の略号であり、次
のようにして求められる。すなわち、試料のX線測定を
行い、得られたX線散乱強度曲線の2θ=17°の散乱
強度りと2θ=25.5°の散乱強度It (いずれ
も空気散乱の値を差し引いた値)から次式を用いて算出
される。(図面参照)
ここで
2
■1は残存アクリロニトリル重合体結晶の量を反映する
ものであり、他方■2はグラファイト構造を反映するも
のである。焼成の進行とともにhが減少し、■2が増加
するのでC,I値は増加していく。C and I are carbonization index (Car
This is an abbreviation for bonization index) and is determined as follows. That is, X-ray measurement of the sample is performed, and the scattering intensity at 2θ = 17° and the scattering intensity It at 2θ = 25.5° of the obtained X-ray scattering intensity curve (both values are values obtained by subtracting the value of air scattering). It is calculated using the following formula. (See drawing) Here, 2 (1) reflects the amount of residual acrylonitrile polymer crystals, while (2) reflects the graphite structure. As firing progresses, h decreases and (2) increases, so the C and I values increase.
本発明者らは、アイソタクチック・トリアッド分率の高
いアクリロニトリル重合体が加水分解を受けやすいこと
を実験的に確認しており、この重合体もしくはこの重合
体からなる繊維を酸水溶液中で加水分解させ、ポリマー
中に環化反応の開始部分としてのアミド基又はカルボキ
シル基を導入することにより、焼成速度を高くすること
も可能にした。酸としては塩酸、硫酸、硝酸、酢酸など
が用いられる。酸水溶液は室温でもよいが加温しておく
ことがより望ましく、低濃度の酸水溶液であれば、高温
に、高濃度の酸水溶液であれば低温でもよい。The present inventors have experimentally confirmed that an acrylonitrile polymer with a high isotactic triad fraction is susceptible to hydrolysis, and this polymer or a fiber made of this polymer was hydrolyzed in an acid aqueous solution. It was also possible to increase the firing rate by decomposing and introducing into the polymer an amide group or carboxyl group as an initiator of the cyclization reaction. As the acid, hydrochloric acid, sulfuric acid, nitric acid, acetic acid, etc. are used. Although the acid aqueous solution may be at room temperature, it is more desirable to heat it.If the acid aqueous solution has a low concentration, it may be heated at a high temperature, and if the acid aqueous solution has a high concentration, it may be heated at a low temperature.
本発明で得られた炭素繊維は、高強力、高弾性であるた
め、産業資材分野、複合材料原料分野、宇宙工学分野な
どにおいても、種々の用途に有用である。同時に、焼成
が速いため生産性が高い。Since the carbon fiber obtained by the present invention has high strength and high elasticity, it is useful for various applications such as in the field of industrial materials, raw materials for composite materials, and space engineering. At the same time, productivity is high due to fast firing.
〈実施例〉
以下、実施例に従って本発明をさらに具体的に説明する
。<Examples> The present invention will now be described in more detail with reference to Examples.
実施例1
アイソタクチック・トリアッド分率が0.52の前述の
有機金属触媒法により得られたアクリロニトリル重合体
をO″Cに保ったままの環境において、70重量%硝酸
水溶液に15重量%濃度で溶解させたところこの組成物
は紡糸に好適な曳糸性を示した。Example 1 An acrylonitrile polymer obtained by the above-mentioned organometallic catalyst method having an isotactic triad fraction of 0.52 was added to a 70% by weight nitric acid aqueous solution at a concentration of 15% by weight in an environment maintained at O''C. When dissolved, this composition exhibited stringiness suitable for spinning.
この紡糸原液を33.0重量%硝酸水溶液よりなる凝固
液中に孔径0.18 mm、孔数40の紡口より吐出し
、凝固させ、95°Cの熱水中で3.0倍、150 ”
Cの乾熱ロールで3.2倍延伸した。次いで、この繊維
を空気中250°Cで、4時間焼成すると、C,I値が
0.56の耐炎化糸が得られた。This spinning stock solution was discharged into a coagulating solution consisting of a 33.0 wt% nitric acid aqueous solution through a spinneret with a pore diameter of 0.18 mm and a number of holes of 40, and coagulated, and then heated 3.0 times in hot water at 95° C. ”
It was stretched 3.2 times with a dry heat roll of C. Next, this fiber was fired in air at 250° C. for 4 hours to obtain a flame-resistant yarn with a C,I value of 0.56.
その後、この耐炎化糸を窒素中400〜1400°Cで
炭化処理したところ強度603 kg/d、弾性率38
.47on/−の炭素繊維が得られた。Afterwards, this flame-resistant yarn was carbonized at 400 to 1400°C in nitrogen, resulting in a strength of 603 kg/d and an elastic modulus of 38.
.. 47 on/- carbon fibers were obtained.
実施例2
アイソタクチック・トリアッド分率が0.37の有機金
属触媒法によるアクリロニトリル重合体を実施例1と同
様の方法で紡糸、耐炎化を行うと、C,I値が0.55
の耐炎化糸が得られた。Example 2 When an acrylonitrile polymer produced by an organometallic catalyst method with an isotactic triad fraction of 0.37 was spun and flame-resistant in the same manner as in Example 1, the C,I value was 0.55.
A flame-resistant yarn was obtained.
その後、この耐炎化糸を窒素中400〜1400″Cで
炭化処理したところ強度502 kg/mj、弾性率3
0.ITon/−の炭素繊維が得られた。Thereafter, this flame-resistant yarn was carbonized at 400 to 1400''C in nitrogen, resulting in a strength of 502 kg/mj and an elastic modulus of 3.
0. Carbon fibers of Iton/- were obtained.
実施例3
アイソタクチック・トリアッド分率が0.60のγ線法
によるアクリロニトリル重合体を実施例1と同様の方法
で紡糸した。但し、凝固液は45.0重量%硝酸水溶液
を用い、その後、溶剤残存状態における延伸として46
.0重量%硝酸水溶液よりなる浴中、58°Cで8.0
倍、熱水中で1.2倍、乾熱ロールで1.9倍延伸した
。次いで、この繊維ヲ空気中250°Cで、4時間焼成
すると、C,I値が0.59の耐炎化糸が得られた。Example 3 An acrylonitrile polymer having an isotactic triad fraction of 0.60 by the gamma ray method was spun in the same manner as in Example 1. However, a 45.0% by weight nitric acid aqueous solution was used as the coagulation solution, and then 46% by weight was used as a stretching method with the solvent remaining.
.. 8.0 at 58°C in a bath consisting of 0% by weight nitric acid aqueous solution.
The film was stretched 1.2 times in hot water and 1.9 times using a dry heat roll. Next, this fiber was fired in air at 250° C. for 4 hours to obtain a flame-resistant yarn with a C,I value of 0.59.
その後、この耐炎化糸を窒素中400〜1400″Cで
炭化処理したところ強度682 kg/d、弾性率42
.2Ton/−の炭素繊維が得られた。Afterwards, this flame-resistant yarn was carbonized at 400 to 1400''C in nitrogen, resulting in a strength of 682 kg/d and an elastic modulus of 42.
.. 2 Ton/- carbon fibers were obtained.
実施例4
実施例工で得たアイソタクチック・トリアッド分率が0
.52の重合体を、濃度2規定の塩酸で20°C30分
処理した重合体を70重量%硝酸水溶液に15重量%濃
度で溶解させ、しかる後その紡糸原液を33.0重量%
硝酸水溶液よりなる凝固液中に孔径0.18mm、孔数
40の紡口より吐出し、凝固させ、95℃の熱水中で2
.5倍、150°Cの乾熱ロールで2.8倍延伸した。Example 4 The isotactic triad fraction obtained in the example process is 0
.. Polymer No. 52 was treated with 2N hydrochloric acid at 20°C for 30 minutes, then dissolved in a 70% aqueous nitric acid solution at a concentration of 15% by weight, and then the spinning stock solution was dissolved at 33.0% by weight.
A coagulating solution consisting of an aqueous nitric acid solution was discharged from a spinneret with a pore diameter of 0.18 mm and a number of holes of 40, coagulated, and then heated in hot water at 95°C for 2 hours.
.. It was stretched 5 times and 2.8 times with a dry heat roll at 150°C.
これを更に実施例1と同様な耐炎化、並びに炭化条件で
炭素繊維となした。その耐炎化糸のC,I値は0.65
、炭化糸の強度は527 kg/lj、弾性率は37
.3 Ton/−であった。This was further made into carbon fiber under the same flame resistance and carbonization conditions as in Example 1. The C and I values of the flame-resistant yarn are 0.65
, the strength of the carbonized yarn is 527 kg/lj, and the elastic modulus is 37
.. It was 3 Ton/-.
実施例5
実施例1で用いたアクリロニトリル重合体からなる繊維
をやはり濃度2規定の塩酸で20°C30分処理した繊
維を実施例1と同様に耐炎化及び炭化した。耐炎化糸の
C8■値は0.62 、炭化糸の強度591 )cg/
d、弾性率36.67on/−であった。Example 5 The fibers made of the acrylonitrile polymer used in Example 1 were also treated with 2N hydrochloric acid at 20°C for 30 minutes, and the fibers were flame-resistant and carbonized in the same manner as in Example 1. The C8 value of the flame-resistant yarn is 0.62, and the strength of the carbonized yarn is 591) cg/
d, the elastic modulus was 36.67 on/-.
実施例6
実施例1で得たアイソタクチック・トリアッド分率が0
.52の重合体を、9.0重量%の塩化リチウムを含有
するジメチルホルムアごドに溶解して、ジメチルホルム
アミド45重量%水溶液の凝固浴中に実施例1と同様の
紡口より吐出したところ、紡糸は極めて順調に行うこと
が出来た。この繊維を更に実施例1と同様な延伸処理条
件および耐炎化、炭化条件で炭素繊維とした。その耐炎
化糸のc、r値は0.62 、炭化糸の強度は573
kg7sノ、弾性率は39.47on/−となった。Example 6 The isotactic triad fraction obtained in Example 1 is 0
.. When the polymer No. 52 was dissolved in dimethylformamide containing 9.0% by weight of lithium chloride and discharged from the same spindle as in Example 1 into a coagulation bath of a 45% by weight aqueous solution of dimethylformamide, Spinning could be carried out extremely smoothly. This fiber was further made into carbon fiber under the same stretching conditions, flame resistance, and carbonization conditions as in Example 1. The c and r values of the flame-resistant yarn are 0.62, and the strength of the carbonized yarn is 573.
kg7s, the elastic modulus was 39.47 on/-.
実施例7
実施例1で得たアイソタクチック・トリアッド分率が0
.52の重合体を、ロダン酸ナトリウム50重量%水溶
液に溶解して、やはりロダン酸ナトリウム12重量%水
溶液の凝固浴中に実施例1と同様の紡口より吐出したが
、紡糸は極めて良好に行われた。この繊維を更に実施例
1と同様な延伸処理条件および耐炎化、炭化条件で炭素
繊維としたところ、その耐炎化糸のC,I値は0.58
、炭化糸の強度は586 kg/mj、弾性率は36.
8 Ton/−となった。Example 7 The isotactic triad fraction obtained in Example 1 is 0
.. The polymer No. 52 was dissolved in a 50% by weight aqueous solution of sodium rhodanate and discharged from the same spinneret as in Example 1 into a coagulation bath of a 12% by weight aqueous sodium rhodanate solution, but spinning was performed extremely well. I was disappointed. When this fiber was further made into carbon fiber under the same stretching conditions, flame resistant and carbonized conditions as in Example 1, the C and I values of the flame resistant yarn were 0.58.
The strength of the carbonized yarn is 586 kg/mj, and the elastic modulus is 36.
It became 8 Ton/-.
比較例1
AN 94.3重量%、アクリル酸メチル4.5重量%
、メタクリル酸1.2重量%からなる3元ラジカル共重
合体(アクリロニトリル連鎖部分のアイソタクチック・
トリアッド分率は、0.27であった。)をO″Cに保
ったままの環境において、70重量%硝酸水溶液に15
重量%濃度で溶解させ、この紡糸原液を33重量%硝酸
水溶液よりなる凝固液中に孔径0.075 ym、孔数
3000の紡口より吐出し、凝固させ、12倍に延伸し
た。次いで、実施例1と同様に耐炎化及び炭化した。耐
炎化糸のC,I値は0.55、炭化糸の強度は400
kg/lj、弾性率は24.5 Ton/−であった。Comparative Example 1 AN 94.3% by weight, methyl acrylate 4.5% by weight
, a tertiary radical copolymer consisting of 1.2% by weight of methacrylic acid (isotactic of the acrylonitrile chain part)
The triad fraction was 0.27. ) in a 70% by weight nitric acid aqueous solution in an environment where the temperature is maintained at O''C.
The spinning stock solution was discharged from a spinneret with a pore diameter of 0.075 ym and 3000 holes into a coagulating solution consisting of a 33 wt % nitric acid aqueous solution, coagulated, and stretched 12 times. Next, flame resistance and carbonization were performed in the same manner as in Example 1. The C and I values of the flame-resistant yarn are 0.55, and the strength of the carbonized yarn is 400.
kg/lj, and the elastic modulus was 24.5 Ton/-.
図面は耐炎化糸のX線散乱強度曲線を示す図である。 The drawing is a diagram showing an X-ray scattering intensity curve of a flame-resistant yarn.
Claims (1)
ルモノマー連鎖部分のアイソタクチック・トリアッド分
率が少なくとも0.35である立体規則性アクリロニト
リル重合体からなる繊維を原料とすることを特徴とする
炭素繊維の製法^1^3 A carbon fiber characterized by being made from a fiber made of a stereoregular acrylonitrile polymer having an isotactic triad fraction of an acrylonitrile monomer chain portion of at least 0.35 as determined by C-NMR. Manufacturing method
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1-128766 | 1989-05-24 | ||
| JP12876689 | 1989-05-24 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0376823A true JPH0376823A (en) | 1991-04-02 |
Family
ID=14992944
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12545990A Pending JPH0376823A (en) | 1989-05-24 | 1990-05-17 | Production of acrylonitrile polymer-based carbon fiber |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0376823A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2004065434A1 (en) * | 2003-01-23 | 2004-08-05 | Teijin Limited | Polymer for carbon fiber precursor |
| CN100415780C (en) * | 2003-01-23 | 2008-09-03 | 帝人株式会社 | Polymers for carbon fiber precursors |
| JP2010053468A (en) * | 2008-08-27 | 2010-03-11 | Toray Ind Inc | Method for producing carbon fiber precursor fiber |
| JP2011195362A (en) * | 2010-03-18 | 2011-10-06 | Teijin Ltd | Carbon material and method for producing the same |
| CN103409854A (en) * | 2013-08-28 | 2013-11-27 | 西安元创化工科技股份有限公司 | Production method of carbon fiber |
| JP2017531104A (en) * | 2014-10-08 | 2017-10-19 | ジョージア テック リサーチ コーポレイション | High strength and high modulus carbon fiber |
-
1990
- 1990-05-17 JP JP12545990A patent/JPH0376823A/en active Pending
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2004065434A1 (en) * | 2003-01-23 | 2004-08-05 | Teijin Limited | Polymer for carbon fiber precursor |
| US7338997B2 (en) | 2003-01-23 | 2008-03-04 | Teijin Limited | Polymer for carbon fiber precursor |
| CN100415780C (en) * | 2003-01-23 | 2008-09-03 | 帝人株式会社 | Polymers for carbon fiber precursors |
| JP2010053468A (en) * | 2008-08-27 | 2010-03-11 | Toray Ind Inc | Method for producing carbon fiber precursor fiber |
| JP2011195362A (en) * | 2010-03-18 | 2011-10-06 | Teijin Ltd | Carbon material and method for producing the same |
| CN103409854A (en) * | 2013-08-28 | 2013-11-27 | 西安元创化工科技股份有限公司 | Production method of carbon fiber |
| JP2017531104A (en) * | 2014-10-08 | 2017-10-19 | ジョージア テック リサーチ コーポレイション | High strength and high modulus carbon fiber |
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