JP3039080B2 - Method for determining spinning conditions for carbon fiber - Google Patents

Method for determining spinning conditions for carbon fiber

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Publication number
JP3039080B2
JP3039080B2 JP3345956A JP34595691A JP3039080B2 JP 3039080 B2 JP3039080 B2 JP 3039080B2 JP 3345956 A JP3345956 A JP 3345956A JP 34595691 A JP34595691 A JP 34595691A JP 3039080 B2 JP3039080 B2 JP 3039080B2
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JP
Japan
Prior art keywords
pitch
time
spinning
deformation speed
relaxation time
Prior art date
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JP3345956A
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Japanese (ja)
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JPH05179515A (en
Inventor
隆一 原
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Mitsubishi Chemical Corp
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Mitsubishi Chemical Corp
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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明はピッチ系炭素繊維の紡糸
条件決定法に関するものである。この方法によれば、例
えば改善された弾性率を発現するようにピッチ繊維の配
向性を制御することができる。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for determining spinning conditions for pitch-based carbon fibers. According to this method, for example, the orientation of pitch fibers can be controlled so as to exhibit an improved elastic modulus.

【0002】[0002]

【従来の技術】炭素繊維は、比強度、比弾性率が高い材
料で、高性能複合材料のフィラー繊維として最も注目さ
れている。中でもピッチ系炭素繊維は原料が潤沢であ
る、炭化行程の歩留りが大きい、繊維の弾性率が高いな
ど、ポリアクリロニトリル系炭素繊維に比べて様々な利
点を持っている。
2. Description of the Related Art Carbon fiber is a material having a high specific strength and a specific elastic modulus, and is most attracting attention as a filler fiber of a high-performance composite material. Among them, pitch-based carbon fibers have various advantages as compared with polyacrylonitrile-based carbon fibers, such as abundant raw materials, a high yield in the carbonization process, and a high elastic modulus of the fibers.

【0003】周知のように重質油、タール、ピッチ等の
炭素原料を350〜500℃に加熱すると、それらの物質中
に、直径が数μmの偏光下に光学的異方性を示す小球体
が生成する。更に加熱するとこれらの小球体は合体、成
長し、最終的に全体が光学的異方性を示す状態となる。
この異方性組織は、炭素質原料の熱重縮合反応により生
成した平面状高分子である芳香族炭化水素が層状に積み
重なり、配向したもので、黒鉛結晶構造の前駆体と見な
されている。
[0003] As is well known, when a carbon material such as heavy oil, tar, pitch or the like is heated to 350 to 500 ° C, small spheres having an optical anisotropy under polarized light having a diameter of several µm are included in those materials. Is generated. Upon further heating, these small spheres coalesce and grow, eventually reaching a state in which the whole exhibits optical anisotropy.
This anisotropic structure is obtained by stacking and orienting aromatic hydrocarbons, which are planar macromolecules generated by a thermal polycondensation reaction of a carbonaceous raw material, in a layered manner, and is regarded as a precursor of a graphite crystal structure.

【0004】このような異方性組織を含む熱処理物は、
一般にメソフェーズピッチと呼称されている。かかるメ
ソフェーズピッチを紡糸ピッチとし、紡糸ノズルを通し
て溶融紡糸することによりピッチ繊維を得ることができ
る。
A heat-treated product containing such an anisotropic structure is
It is generally called a mesophase pitch. A pitch fiber can be obtained by using such a mesophase pitch as a spinning pitch and melt-spinning through a spinning nozzle.

【0005】[0005]

【発明が解決しようとする課題】上記のように配向性の
よい紡糸原料であるメソフェーズピッチを用いて高弾性
率の炭素繊維を製造することができる。通常、より高い
弾性率の炭素繊維を製造するためには、ピッチ繊維を不
融化、続いて炭化、黒鉛化する焼成過程において、より
高い焼成温度を必要とする。これは生産上不利な条件で
あり紡糸条件を変更してピッチ繊維の配向性を向上させ
て解決する方法がとられてきた。しかしながら、紡糸の
操作因子は多岐に渡り、ノズル径、ピッチ繊維径、吐出
するピッチの温度と速度、巻取り速度、ノズル直下の雰
囲気の温度等の冷却条件などをすべて個別に勘案しなけ
ればならず、所望のピッチ繊維を製造するための最適条
件の選択が困難であるという問題点があった。本発明は
この問題点を解決する。
As described above, a carbon fiber having a high elastic modulus can be produced using mesophase pitch which is a spinning raw material having good orientation. Generally, in order to produce carbon fibers having a higher elastic modulus, a higher firing temperature is required in a firing process in which pitch fibers are made infusible, subsequently carbonized and graphitized. This is a disadvantageous condition in production, and a method of solving the problem by changing the spinning conditions to improve the orientation of pitch fibers has been adopted. However, the operating factors of spinning vary widely, and cooling conditions such as the nozzle diameter, the pitch fiber diameter, the temperature and speed of the discharged pitch, the winding speed, the temperature of the atmosphere directly below the nozzle, etc., must be individually considered. In addition, there is a problem that it is difficult to select optimum conditions for producing a desired pitch fiber. The present invention solves this problem.

【0006】[0006]

【課題を解決するための手段】そこで、本発明者らはか
かる点に留意し、鋭意検討した結果、紡糸ピッチの緩和
時間と紡糸プロセスにおける代表時間との比であるデボ
ラ数を用いて紡糸条件を決定すれば所定の配向角を有す
るピッチ繊維を容易に決定できることを見いだした。
The inventors of the present invention have paid careful attention to such a point, and as a result of intensive studies, have found that the spinning conditions are determined by using the Deborah number, which is the ratio between the relaxation time of the spinning pitch and the representative time in the spinning process. Determined that pitch fibers having a predetermined orientation angle can be easily determined.

【0007】加熱溶融したピッチを、紡糸してピッチ繊
維を得、次いで不融化処理し、更に炭化および/または
黒鉛化して炭素繊維を製造するに当たり、溶融ピッチを
細孔から吐出させて細径化させる溶融紡糸において、溶
融ピッチの変形速度が最大となる近傍におけるプロセス
の代表時間tと、溶融ピッチの変形速度が最大となる近
傍におけるピッチの緩和時間τとを求めて、下記式
(I)に従ってデボラ数NDを算出し、デボラ数NDを用
いて、所望の炭素繊維の配向性を制御するための紡糸の
条件を決定することができる。
[0007] The heated and melted pitch is spun to obtain pitch fibers, then subjected to infusibilization treatment, and further carbonized and / or graphitized to produce carbon fibers. In the melt spinning to be performed, the representative time t of the process in the vicinity where the deformation speed of the molten pitch is maximum and the relaxation time τ of the pitch in the vicinity where the deformation speed of the molten pitch is maximum are determined according to the following formula (I). calculating a Deborah number N D, using the Deborah number N D, it is possible to determine the spinning conditions for controlling the orientation of the desired carbon fibers.

【0008】[0008]

【数2】ND=τ/t (I) 以下、本発明を説明するに、本発明で用いる紡糸ピッチ
は、配向し易い分子種が形成されており、光学的に異方
性の炭素繊維を与える様なものであれば特に制限はな
い。これらの紡糸ピッチを得るための炭素質原料として
は、例えば、石炭系のコールタール、コールタールピッ
チ、石炭液化物、石油系の重質油、タール、ピッチ、等
があげられる。これらの炭素質原料には、通常、フリー
カーボン、未溶解石炭、灰分等の不純物が含まれている
が、これらの不純物は、濾過、遠心分離、あるいは溶剤
を使用する靜置沈降分離等の周知の方法で予め除去して
おくことが望ましい。また、炭素質原料として、例え
ば、加熱処理した後、特定溶剤で可溶分を抽出するとい
った方法、あるいは水素供与性溶剤、水素ガスの存在下
に水添処理するといった方法で予備処理を行っておいて
もよい。
[Number 2] N D = τ / t (I ) below, in describing the present invention, the spinning pitch used in the present invention, oriented it is likely molecular species forming an optically anisotropic carbon fiber There is no particular limitation as long as it gives. Examples of the carbonaceous raw material for obtaining these spinning pitches include coal-based coal tar, coal-tar pitch, coal liquefaction, petroleum heavy oil, tar, pitch, and the like. These carbonaceous raw materials usually contain impurities such as free carbon, undissolved coal, and ash, and these impurities are well-known in the art such as filtration, centrifugation, or stationary sedimentation using a solvent. It is desirable to remove in advance by the above method. Further, as a carbonaceous raw material, for example, after a heat treatment, a preliminary treatment is performed by a method of extracting a soluble component with a specific solvent, or a method of hydrogenating in the presence of a hydrogen-donating solvent or hydrogen gas. You may leave.

【0009】前記炭素質原料あるいは予備処理を行った
炭素質原料を、ついで、通常、350〜500℃、好ま
しくは380〜450℃で、2分〜50時間、好ましく
は5分〜5時間の範囲で適宜条件を選択して、窒素、ア
ルゴン等の不活性ガス雰囲気下、或は、吹き込み下に加
熱処理することに依って得られる40%以上、好ましく
は70%以上の光学的異方性組織を含むメソフェーズピ
ッチが好適に使用できる。
The carbonaceous raw material or the carbonaceous raw material which has been subjected to the pretreatment is then treated at 350 to 500 ° C., preferably 380 to 450 ° C., for 2 minutes to 50 hours, preferably 5 minutes to 5 hours. Conditions are appropriately selected, and an optically anisotropic structure of 40% or more, preferably 70% or more obtained by heat treatment in an atmosphere of an inert gas such as nitrogen or argon, or under blowing. Can be suitably used.

【0010】本発明でいうメソフェーズピッチの光学的
異方性割合は、常温下の偏光顕微鏡観察により求めた光
学的異方性割合を示す部分の面積割合である。具体的に
は、直径数mmのメソフェーズピッチ粒多数を、埋め込
み樹脂に包埋し、表面を研磨した後、ピッチ研磨面全体
をくまなく偏光顕微鏡観察(100倍)し、全面積に対
する光学異方性部分の面積割合を測定することによって
求める。
The optical anisotropy ratio of the mesophase pitch referred to in the present invention is the area ratio of the portion showing the optical anisotropy ratio obtained by observation with a polarizing microscope at normal temperature. More specifically, after embedding a large number of mesophase pitch grains having a diameter of several mm in an embedding resin and polishing the surface, the entire pitch polished surface is observed with a polarizing microscope (100 times) throughout, and the optical anisotropy with respect to the entire area is measured. It is determined by measuring the area ratio of the sex part.

【0011】上記のようなピッチを、紡糸してピッチ繊
維を得、次いで不融化処理し、更に炭化および/または
黒鉛化して炭素繊維を製造するに当たり、溶融ピッチを
細孔から吐出させて細径化させる溶融紡糸において、溶
融ピッチの変形速度dV(x)/dxが最大となる近傍
におけるプロセスの代表時間tと、溶融ピッチの変形速
度dV(x)/dxが最大となる近傍におけるおけるピ
ッチの緩和時間τとを求めて、下記式(I)に従ってデ
ボラ数NDを算出し、デボラ数NDをもちいて、所望の炭
素繊維の配向性を制御するための紡糸の条件を決定す
る。ここでxは、ノズル吐出部を原点として走行糸方向
の距離、V(x)は、位置xの走行糸の速度である。
The pitch as described above is spun to obtain pitch fibers, then subjected to infusibilization treatment, and further carbonized and / or graphitized to produce carbon fibers. In the melt spinning to be formed, the representative time t of the process in the vicinity where the deformation speed dV (x) / dx of the molten pitch is maximum, and the pitch in the vicinity where the deformation speed dV (x) / dx of the molten pitch is maximum. seeking the relaxation time tau, calculates the Deborah number N D according to the following formula (I), the using a Deborah number N D, determining the spinning conditions for controlling the orientation of the desired carbon fibers. Here, x is the distance in the traveling yarn direction with the nozzle discharge portion as the origin, and V (x) is the velocity of the traveling yarn at the position x.

【0012】[0012]

【数3】ND=τ/t (I) ここでいう変形速度 (dV(x)/dx)の値は、ノ
ズルからの位置xにおける速度勾配であるが、変形速度
の意味を持っている。いまdxの区間をdtの時間で通
過する時に、速度がdV増加したとする。dV・dt/
dxは、dtの間に受けた伸び歪であるから、
N D = τ / t (I) The value of the deformation speed (dV (x) / dx) here is a speed gradient at the position x from the nozzle, but has a meaning of the deformation speed. . Now, suppose that the speed increases by dV when passing through the section of dx at the time of dt. dV · dt /
Since dx is the elongation strain received during dt,

【0013】[0013]

【数4】dV・dt/dx×1/dt= dV/dx 従って(dV(x)/dx)の値は伸長歪の速度であ
る。以下に近傍の定義を示す。図1に示したように、変
形速度の最大値の位置x2をはさんで2点x1、x3を取
ったときx1とx2とを両端とする領域をx2の近傍とす
る。x1、x3は最大変形速度の70%以上のの変形速度
の位置、好ましくは、80%以上の変形速度の位置が望
ましい。
## EQU4 ## dV ・ dt / dx × 1 / dt = dV / dx Therefore, the value of (dV (x) / dx) is the rate of elongation strain. The definition of the neighborhood is shown below. As shown in FIG. 1, the region of both ends of the x 1 and x 2 and the vicinity of the x 2 when taking two points x 1, x 3 across the position x 2 of the maximum value of the deformation speed . x 1 and x 3 are preferably at positions where the deformation speed is 70% or more of the maximum deformation speed, preferably at positions where the deformation speed is 80% or more.

【0014】以下に紡糸プロセスの代表時間の定義を示
す。紡糸プロセスの代表時間は、紡糸が速い(短時間)
か、遅い(長時間)かを表す指標である。代表時間の決
め方は種々考えられるが、本発明では、ピッチ繊維さら
には炭素繊維の物性値に最も影響する時間として、変形
速度が最大となる位置またはその近傍において経過する
時間を代表時間として採用する。
The definition of the representative time of the spinning process is shown below. Typical spinning process time is fast spinning (short time)
Or a slow (long) time. Although various methods for determining the representative time are conceivable, in the present invention, as the time that most affects the physical properties of the pitch fiber and the carbon fiber, the time that elapses at or near the position where the deformation speed is the maximum is adopted as the representative time. .

【0015】変形速度の最大値の逆数は、この位置にお
いて走行糸が最高速度で細長く変形して行くときの、単
位歪当りの経過時間である。変形速度の最大値の近傍の
平均変形速度の逆数についてもこの近傍における単位歪
当りの経過時間である。定義された所定の近傍を通過す
る時間を代表時間としてもよい。次に紡糸プロセスの代
表時間の求め方について説明する。
The reciprocal of the maximum value of the deformation speed is the elapsed time per unit strain when the running yarn is slenderly deformed at the maximum speed at this position. The reciprocal of the average deformation speed near the maximum value of the deformation speed is also the elapsed time per unit strain in this vicinity. The time passing through the defined predetermined neighborhood may be used as the representative time. Next, how to determine the representative time of the spinning process will be described.

【0016】紡糸プロセスの代表時間はノズルから吐出
された溶融ピッチが細径化し、固化してピッチ繊維にな
るときの直径の変化を測定することに依って求めること
もできる。ノズルから吐出されるときの線速度V0、ノ
ズル径D0とし、ノズルからの距離xにおける繊維径D
(x)とすると位置xに於ける線速度Vは、
The representative time of the spinning process can also be determined by measuring the change in diameter when the molten pitch discharged from the nozzle is reduced in diameter and solidified into pitch fibers. The linear velocity V 0 at the time of discharge from the nozzle, the nozzle diameter D 0, and the fiber diameter D at a distance x from the nozzle
Assuming (x), the linear velocity V at the position x is

【0017】[0017]

【数5】V(x)=V0(D0/D(x))2 として計算することができる。図2に点線で結果を定性
的に示した。V(x)を微分してdV(x)/dxの値
を図2の実線のように求めることができる。直径の測定
と同時に、後述する様に、走行糸上の緩和時間を求める
必要から、図2の破線で示したようにこの細径化過程に
おける走行糸の温度を知る必要がある。
## EQU5 ## It can be calculated as V (x) = V 0 (D 0 / D (x)) 2 . FIG. 2 qualitatively shows the results by dotted lines. By differentiating V (x), the value of dV (x) / dx can be obtained as shown by the solid line in FIG. Simultaneously with the measurement of the diameter, as will be described later, it is necessary to obtain the relaxation time on the running yarn. Therefore, as shown by the broken line in FIG.

【0018】実測で求める方法は、顕微鏡付きカメラ等
で糸径の変化を測定し、赤外線温度計で温度変化を測定
することが可能である。しかしこの方法は、多大な時間
を要し、かつ、精度ある測定が困難なので、シミュレー
ションによって計算することが望ましい。加瀬、松尾ら
は、図2に示した内容をシミュレーションで求める方法
を提案している(J. Polymer Sci. Part A, 3. 2541(19
65))。これによると、ピッチの物性値として粘度と密
度の温度依存性を与え、紡糸条件として、ノズル径、吐
出ピッチの温度、線速度、巻取速度、ノズル下雰囲気の
温度と気流の速度を与えて、図2に示したようにノズル
下の距離xに対する変形速度dV(x)/dxと温度T
(x)の値を知ることができる。この結果から以下の内
容の紡糸プロセスの代表時間tを求め、用いることがで
きる。
As a method of actual measurement, it is possible to measure a change in the yarn diameter with a camera equipped with a microscope or the like, and to measure a temperature change with an infrared thermometer. However, this method requires a great deal of time, and it is difficult to perform accurate measurement. Kase, Matsuo et al. Have proposed a method of obtaining the contents shown in Fig. 2 by simulation (J. Polymer Sci. Part A, 3. 2541 (19
65)). According to this, the temperature dependence of viscosity and density is given as the physical property value of the pitch, and the nozzle diameter, the temperature of the discharge pitch, the linear speed, the winding speed, the temperature of the atmosphere under the nozzle and the airflow speed are given as the spinning conditions. 2, the deformation speed dV (x) / dx and the temperature T with respect to the distance x below the nozzle as shown in FIG.
The value of (x) can be known. From this result, a representative time t of the spinning process having the following contents can be obtained and used.

【0019】変形速度の最大値(dV(x)/dx)ma
xの逆数値。図1に示したように(dV(x)/dx)m
axを示す位置x2をはさんで、近傍x1からx3間の経過
時間。前記x1からx3までのdV(x)/dxの値の平
均値(dV(x)/dx)aveの逆数値。
The maximum value of the deformation speed (dV (x) / dx) ma
Reciprocal value of x. As shown in FIG. 1, (dV (x) / dx) m
across the position x2 indicating the ax, the elapsed time between x 3 from the vicinity x 1. Inverse value of the average value of dV (x) / dx from x 1 to x 3 (dV (x) / dx) ave.

【0020】更に緩和時間の求め方について説明する。
粘弾性測定機を用いて振動法で溶融ピッチの粘弾性を測
定することにより緩和時間を求めることができる。すな
わち、図3に示したように、ピッチのガラス転位温度近
傍で、温度一定の条件で角周波数を変更して動的損失
G”を測定すると、G”の角周波数依存性は上に凸とな
る。G”が極大値G”maxを示す時の角周波数の逆数の
値は、この測定温度に於ける緩和時間τとなる。測定温
度を変更することにより緩和時間の温度依存性をもとめ
ることができる。温度が高いために極大値が測定温度で
得られない場合は、図3の矢印で示したように、極大値
を有する低温側の角周波数依存性の曲線を、時間ー温度
換算則に基づいて角周波数軸に添ってシフトすることに
よって、極大値を測定できなかった温度における緩和時
間τを求めることができる。本発明では、粘弾性測定装
置として振動法の測定装置レオメトリックスRDS−II
を用いた。知られているように振動法のほかステップ状
の応力を与える応力緩和法でも、緩和時間τの温度依存
性を求めることができる。緩和時間τはピッチの物性値
であり、上述の様に温度Tの関数として一義的に求める
ことができる。具体的には、緩和時間τとして、図1に
示した変形速度の最大値(dV(x)/dx)maxの位
置における温度T2の緩和時間τ(T2)、図1に示した
ように(dV(x)/dx)maxを示す位置x2をはさむ
近傍の位置、x1からx3まで温度T1からT3の平均値T
aveにおける緩和時間τ(Tave)を用いることができ
る。T2、Tave以外の温度における緩和時間を用いるこ
とは望ましくない。
Further, a method of obtaining the relaxation time will be described.
The relaxation time can be determined by measuring the viscoelasticity of the molten pitch by a vibration method using a viscoelasticity measuring device. That is, as shown in FIG. 3, when the dynamic loss G ″ is measured near the glass transition temperature of the pitch and the angular frequency is changed under a constant temperature condition, the angular frequency dependency of G ″ is upwardly convex. Become. The value of the reciprocal of the angular frequency when G ″ indicates the maximum value G ″ max is the relaxation time τ at the measured temperature. By changing the measurement temperature, the temperature dependence of the relaxation time can be determined. When the maximum value cannot be obtained at the measurement temperature due to the high temperature, as shown by the arrow in FIG. 3, the curve of the angular frequency dependence on the low temperature side having the maximum value is calculated based on the time-temperature conversion rule. By shifting along the angular frequency axis, the relaxation time τ at the temperature where the maximum value could not be measured can be obtained. In the present invention, as a viscoelasticity measuring device, a measuring device of the vibration method Rheometrics RDS-II is used.
Was used. As is known, the temperature dependence of the relaxation time τ can be obtained by a stress relaxation method that applies a step-like stress in addition to the vibration method. The relaxation time τ is a physical property value of the pitch, and can be uniquely obtained as a function of the temperature T as described above. Specifically, as the relaxation time τ, the relaxation time τ (T 2 ) of the temperature T 2 at the position of the maximum value of the deformation speed (dV (x) / dx) max shown in FIG. 1, as shown in FIG. the (dV (x) / dx) position near to sandwich the position x2 indicating the max, mean value of T 3 from temperature T 1 of from x 1 to x 3 T
The relaxation time τ (Tave) at ave can be used. It is undesirable to use relaxation times at temperatures other than T 2 and Tave.

【0021】デボラ数NDは、前述した緩和時間τと紡
糸プロセスの代表時間tの比τ/tとして求めることが
できる。これはピッチという物質の持っている固有の時
間スケールと、紡糸というプロセスが持っている変形の
時間スケールと両者の長短を相対的に比較することに相
当し、緩和時間τが相対的に短ければ、溶融ピッチが紡
糸行程で伸長される時に発生する弾性力が緩和して、ピ
ッチ繊維の中に残留応力として残らないことを意味し、
緩和時間τが相対的に長ければ弾性力は緩和できないま
までピッチ繊維の中に凍結されることを意味する。この
内容がピッチ繊維の分子の配向性、ひいては炭素繊維の
グラファイト網面の配向性を支配する。
The Deborah number N D can be obtained as the ratio τ / t between the relaxation time τ and the representative time t of the spinning process. This is equivalent to comparing the inherent time scale of the pitch material with the deformation time scale of the spinning process and the length of the two, and if the relaxation time τ is relatively short, , Means that the elastic force generated when the molten pitch is elongated in the spinning process is relaxed and does not remain as residual stress in the pitch fiber,
If the relaxation time τ is relatively long, it means that the elastic force is frozen in the pitch fibers without being relaxed. This content governs the orientation of the molecules of the pitch fiber and thus the orientation of the graphite network of the carbon fiber.

【0022】デボラ数NDの値は走行糸上の全ての位置
で求めることはできるが、検討の結果、ピッチ繊維の配
向性を直接決定するデボラ数NDとして、(dV(x)
/dx)maxの位置もしくはその近傍の位置の値を使用
するのが好ましいことが判明した。その他の位置におけ
るデボラ数NDを用いることは好ましくない。デボラ数
とピッチ繊維の配向性の関係として図4に紡糸して得た
ピッチ繊維の配向角とデボラ数との関係を示した。ここ
では、デボラ数は、代表時間tとして、変形速度の最大
値 (dV(x)/dx)maxの逆数値を用い、緩和時
間τとして、変形速度の最大値 (dV(x)/dx)
maxの位置における温度に対応する緩和時間の値を用い
て求めた。
[0022] While the value of the Deborah number N D can be determined at all positions on the traveling yarn, the result of the study, as Deborah number N D of determining the orientation of pitch fibers directly, (dV (x)
It has been found that it is preferable to use the value of the position at or near / dx) max. The use of the Deborah number N D at other positions are not preferred. FIG. 4 shows the relationship between the orientation angle of the pitch fiber obtained by spinning and the Deborah number as the relationship between the Deborah number and the orientation of the pitch fiber. Here, as the Deborah number, the reciprocal value of the maximum value of the deformation speed (dV (x) / dx) max is used as the representative time t, and the maximum value of the deformation speed (dV (x) / dx) is used as the relaxation time τ.
It was determined using the value of the relaxation time corresponding to the temperature at the position of max.

【0023】代表時間tとして、図1に示した、x1
らx3までの経過時間を用いてもよい。また、代表時間
tとして前記x1からx3までの(dV(x)/dx)av
eの逆数を用いてもよい。緩和時間τとして、図1のx1
からx3まで平均温度Taveにおける緩和時間をもちいて
もよい。最も好ましくは、変形速度の最大値の位置でデ
ボラ数NDを決定する方がよい。
The elapsed time from x 1 to x 3 shown in FIG. 1 may be used as the representative time t. Further, as a representative time t from the x 1 to x 3 (dV (x) / dx) av
The reciprocal of e may be used. As the relaxation time τ, x 1 in FIG.
Or by using a relaxation time in the average temperature Tave to x 3 from. Most preferably, it is better to determine the Deborah number N D at the position of the maximum value of the deformation speed.

【0024】ここで配向角ψの測定は集束して揃えたピ
ッチ繊維の束を試料として、繊維X線回折装置を用い
て、002回折のピーク位置を経度方向に走査し、得ら
れた回折強度のピークの半価幅を配向角ψとして使用し
た。ピッチ繊維の配向角が小さい場合は、焼成後の炭素
繊維も配向角が小さくなり、弾性率が改善され易くなる
ので、ピッチ繊維の段階で配向角を小さくすることが好
ましい。
Here, the orientation angle ψ is measured by using a bundle of pitch fibers that have been bundled and aligned as a sample and scanning the peak position of 002 diffraction in the longitudinal direction using a fiber X-ray diffractometer to obtain the obtained diffraction intensity. Was used as the orientation angle ψ. When the orientation angle of the pitch fiber is small, the orientation angle of the fired carbon fiber is also small, and the elastic modulus is easily improved. Therefore, it is preferable to reduce the orientation angle at the stage of the pitch fiber.

【0025】配向角が小さくなる条件は、吐出するピッ
チの粘度が低いこと、吐出速度が低いこと、ピッチ繊維
のテイクアップ速度が低いこと、吐出糸回りの雰囲気温
度が高いこと、吐出糸の冷却風速度が低いこと、等複数
の個別の条件が経験的にしられているが、デボラ数の概
念を使えば、所望の配向角のピッチ繊維を得る条件が総
合的に判断可能となる。図4から判るようにピッチ繊維
の配向角はデボラ数がある値以下では、最小且つ一定値
となるの(図の実施例ではデボラ数=1×10 1以下)
で、配向角の小さなピッチ繊維を生産するための有利な
条件を、この範囲で設定することができる。尚、使用す
るτとtとの組合せを変えるとデボラ数の値は、図4に
おいて左右に平行に移動することとなるので、どの組合
せにするかは固定しなければならない。
The conditions for reducing the orientation angle are that the viscosity of the discharged pitch is low, the discharging speed is low, the take-up speed of the pitch fiber is low, the ambient temperature around the discharging yarn is high, and the cooling of the discharging yarn is performed. Although a plurality of individual conditions such as a low wind speed have been empirically determined, the concept of the Deborah number enables comprehensive determination of conditions for obtaining pitch fibers having a desired orientation angle. Orientation angle of pitch fibers as can be seen from Figure 4 the following values have Deborah number, minimum and a constant value of (Deborah number = 1 × 10 -1 or less in the embodiment of FIG.)
Thus, advantageous conditions for producing pitch fibers having a small orientation angle can be set within this range. When the combination of τ and t used is changed, the value of the Deborah number moves in parallel to the left and right in FIG. 4, so that the combination to be used must be fixed.

【0026】配向角の小さなピッチ繊維を特に必要とし
ない場合は、デボラ数の大きな紡糸条件をえらぶことが
できる。この条件で紡糸したピッチ繊維は、弾性率が向
上しにくいが、焼成行程において繊維同志が融着せずに
しなやかな解繊性のよい炭素繊維束を製造することがで
きる。このようにいずれを選択するかは、デボラ数より
総合的に決定すればよい。デボラ数が大きくなりすぎる
と、紡糸中に応力緩和できず、弾性力によって紡糸張力
が大きくなるので、防止条件として採用できない。
When pitch fibers having a small orientation angle are not particularly required, spinning conditions having a large Deborah number can be selected. Although pitch fibers spun under these conditions are unlikely to have an improved elastic modulus, the fibers do not fuse together during the firing step, and a pliable carbon fiber bundle with good fibrillation properties can be produced. In this way, which one to select may be comprehensively determined from the Deborah number. If the Deborah number is too large, stress cannot be relieved during spinning, and spinning tension increases due to elastic force, so that it cannot be adopted as a preventive condition.

【0027】[0027]

【実施例】図4と表1とに実施例及び比較例を示した。
図4の番号は表1の番号に対応する。実施例の紡糸実験
には、異方性97%のメソフェーズピッチ試料とし、直
径0.1mmのノズルを用いた。
FIG. 4 and Table 1 show examples and comparative examples.
The numbers in FIG. 4 correspond to the numbers in Table 1. In the spinning experiment of the example, a mesophase pitch sample having anisotropy of 97% was used, and a nozzle having a diameter of 0.1 mm was used.

【0028】デボラ数ND計算のために用いた紡糸プロ
セスの代表時間tは、シミュレーションに依って求めた
最大変形速度(dV(x)/dx)maxの逆数であり、
緩和時間τは最大変形速度位置の温度に対応する値であ
る。他のtとτとの合せを用いる時は、デボラ数ND
値が図4の横軸の添って平行に移動し、値が変わること
に留意しなければならない。焼成後に得られる炭素繊維
の配向も改善されているので、ピッチ繊維の配向角によ
って炭素繊維の配向性の良否を判断することができる。
[0028] Representative time t of the spinning process used for the Deborah number N D calculation, the maximum deformation rate was determined by a simulation (dV (x) / dx) is the inverse of the max,
The relaxation time τ is a value corresponding to the temperature at the maximum deformation speed position. When using combined with other t and τ is moved in parallel along the values of Deborah number N D is the horizontal axis in FIG. 4, it should be noted that the value changes. Since the orientation of the carbon fibers obtained after firing is also improved, the quality of the orientation of the carbon fibers can be determined based on the orientation angle of the pitch fibers.

【0029】紡糸の操作条件を変更してもデボラ数は一
本の曲線上に乗るので、この値により所望の配向角のピ
ッチ繊維ひいては炭素繊維を得ることができる。すなわ
ち、配向性の改善されたピッチ繊維をうるためには、実
施例1から5のデボラ数となるように吐出温度、巻取速
度などの紡糸条件を決めることができる。高配向性を必
要とせず、解繊性を重要視する場合は、実施例6から7
の条件のデボラ数となるような紡糸条件を決めることが
できる。実施例8から10条件ではデボラ数が大きす
ぎ、紡糸中に溶融状態の走行糸にかかる張力が大きすぎ
て破断しやすいので、紡糸条件としては望ましくない。
Even if the spinning operation conditions are changed, the Deborah number is on one curve, so that pitch fibers and carbon fibers having a desired orientation angle can be obtained from this value. That is, in order to obtain a pitch fiber having improved orientation, spinning conditions such as a discharge temperature and a winding speed can be determined so as to obtain the Deborah numbers of Examples 1 to 5. When high fibrillation is not required and fibrillation is regarded as important, Examples 6 to 7
The spinning conditions can be determined so as to satisfy the Deborah number of the above condition. Under the conditions of Examples 8 to 10, the Deborah number is too large, and the tension applied to the traveling yarn in the molten state during the spinning is too large to be easily broken, which is not desirable as the spinning condition.

【0030】[0030]

【表1】 [Table 1]

【0031】[0031]

【発明の効果】生産上、焼成温度を低下させてもより改
善された弾性率の炭素繊維を生産するためには配向角の
小さなピッチ繊維を紡糸する必要がある。配向角が小さ
くなる紡糸条件として、吐出するピッチの温度高いこと
を初め、複数の個別の条件が考えられるが、デボラ数の
概念を使えば、所望の配向角のピッチ繊維を得る条件が
総合的に判断可能となる。すなわち、デボラ数がある値
以下となる各種の個別操業条件のうち、優先的に選択し
なければならないノズル径、糸直径、等を決定した後、
所望のデボラ数NDの値に合うように、残りの操作条件
を操業し易い様に選択できる。
According to the present invention, it is necessary to spin pitch fibers having a small orientation angle in order to produce carbon fibers having improved elasticity even when the firing temperature is lowered. As the spinning conditions for reducing the orientation angle, a plurality of individual conditions can be considered, including the fact that the temperature of the ejected pitch is high. However, if the concept of Deborah number is used, the conditions for obtaining pitch fibers having a desired orientation angle are comprehensive. Can be determined. That is, after determining the nozzle diameter, yarn diameter, etc., which must be preferentially selected from among various individual operating conditions in which the Deborah number is a certain value or less,
To match the desired value of Deborah number N D, it can be selected to easily operate the remaining operating conditions.

【0032】また操業と平行して粘弾性測定とシミュレ
ーションを行えば、所望の配向角の紡糸条件を随時決定
することも可能となる。
If viscoelasticity measurement and simulation are performed in parallel with the operation, spinning conditions for a desired orientation angle can be determined at any time.

【図面の簡単な説明】[Brief description of the drawings]

【図1】図1はプロセスの代表時間tの説明図である。FIG. 1 is an explanatory diagram of a representative time t of a process.

【図2】図2は緩和時間τの説明図である。FIG. 2 is an explanatory diagram of a relaxation time τ.

【図3】図3は緩和時間τの求め方の説明図である。FIG. 3 is an explanatory diagram of how to find a relaxation time τ.

【図4】図4はピッチ繊維の配向角とデボラ数NDの関
係を示す説明図である。
FIG. 4 is an explanatory view showing the relationship between the orientation angle and Deborah number N D of pitch fibers.

Claims (6)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 加熱溶融したピッチを、紡糸してピッチ
繊維を得、次いで不融化処理し、更に炭化および/また
は黒鉛化して炭素繊維を製造するに当たり、溶融ピッチ
を細孔から吐出させて細径化させる溶融紡糸において、
溶融ピッチの変形速度が最大となる近傍におけるプロセ
スの代表時間tと、溶融ピッチの変形速度が最大となる
近傍におけるピッチの緩和時間τとを求めて、下記式
(I)に従ってデボラ数 D を算出し、デボラ数 D を用
いて、所望の炭素繊維の配向性を制御するための紡糸の
条件を決定することを特徴とする炭素繊維の紡糸条件決
定法。 【数1】 D =τ/t (I)
1. A pitch melted by heating is spun to obtain a pitch fiber, then subjected to an infusibilization treatment, and further carbonized and / or graphitized to produce a carbon fiber. In melt spinning to make diameter,
A representative time t of the process in the vicinity of the deformation rate is maximum of the melting pitch, seeking and pitch relaxation time τ in the vicinity of the deformation rate is maximized molten pitch, the Deborah number N D according to the following formula (I) calculated, use the Deborah number N D
And determining the spinning conditions for controlling the desired orientation of the carbon fibers. N D = τ / t (I)
【請求項2】 プロセスの代表時間tとして、溶融ピッ
チの変形速度の最大値の逆数を用いる請求項1記載の炭
素繊維の紡糸条件決定法。
2. The method according to claim 1, wherein a reciprocal of the maximum value of the deformation speed of the molten pitch is used as the representative time t of the process.
【請求項3】 緩和時間τとして、溶融ピッチの変形速
度の最大値の位置に置ける緩和時間を用いる請求項1記
載の炭素繊維の紡糸条件決定法。
3. The method for determining spinning conditions for carbon fibers according to claim 1, wherein the relaxation time τ is a relaxation time at the position of the maximum value of the deformation speed of the molten pitch.
【請求項4】 プロセスの代表時間tとして、溶融ピッ
チの最大変形速度の位置を含む所定の近傍の経過時間を
用いる請求項1記載の炭素繊維の紡糸条件決定法。
4. The method for determining spinning conditions for a carbon fiber according to claim 1, wherein an elapsed time in a predetermined vicinity including the position of the maximum deformation speed of the molten pitch is used as the representative time t of the process.
【請求項5】 プロセスの代表時間tとして、溶融ピッ
チの最大変形速度の位置を含む所定の近傍の変形速度の
平均値の逆数を用いる請求項1記載の炭素繊維の紡糸条
件決定法。
5. The method for determining spinning conditions for carbon fibers according to claim 1, wherein a reciprocal of an average value of the deformation speed in a predetermined vicinity including the position of the maximum deformation speed of the molten pitch is used as the representative time t of the process.
【請求項6】 緩和時間τとして、溶融ピッチの最大変
形速度の位置を含む所定の近傍に置ける平均の緩和時間
を用いる請求項1記載の炭素繊維の紡糸条件決定法。
6. The method according to claim 1, wherein an average relaxation time in a predetermined vicinity including a position of a maximum deformation speed of the molten pitch is used as the relaxation time τ.
JP3345956A 1991-12-27 1991-12-27 Method for determining spinning conditions for carbon fiber Expired - Lifetime JP3039080B2 (en)

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Publication Number Publication Date
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JP3039080B2 true JP3039080B2 (en) 2000-05-08

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