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JP2507367B2 - Carbon fiber manufacturing method - Google Patents

Carbon fiber manufacturing method

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Publication number
JP2507367B2
JP2507367B2 JP61283551A JP28355186A JP2507367B2 JP 2507367 B2 JP2507367 B2 JP 2507367B2 JP 61283551 A JP61283551 A JP 61283551A JP 28355186 A JP28355186 A JP 28355186A JP 2507367 B2 JP2507367 B2 JP 2507367B2
Authority
JP
Japan
Prior art keywords
fiber tow
opening
carbon fiber
furnace
straight body
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 - Lifetime
Application number
JP61283551A
Other languages
Japanese (ja)
Other versions
JPS63135521A (en
Inventor
秀実 村田
釼三 伴
隆久 深尾
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.)
Mitsubishi Chemical Corp
Original Assignee
Mitsubishi Chemical Corp
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 Mitsubishi Chemical Corp filed Critical Mitsubishi Chemical Corp
Priority to JP61283551A priority Critical patent/JP2507367B2/en
Publication of JPS63135521A publication Critical patent/JPS63135521A/en
Application granted granted Critical
Publication of JP2507367B2 publication Critical patent/JP2507367B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は炭素繊維の製造方法に係るものであり、更に
詳しくは外気の侵入を防止するように構成された加熱炉
を用いる炭素繊維の製造方法に関するものである。
Description: TECHNICAL FIELD The present invention relates to a method for producing carbon fiber, and more specifically, the production of carbon fiber using a heating furnace configured to prevent the invasion of outside air. It is about the method.

(従来技術) 炭素繊維を製造するには、一般に有機重合体、例えば
ポリアクリロニトリル、セルローズ、石油系ピツチ又は
石炭系ピツチを紡糸し集束して得られた繊維トウを酸化
性雰囲気中で150〜400℃に加熱して耐炎化処理又は不融
化処理を行つた後不活性ガス中で500〜1500℃に加熱し
て炭化処理を行い、更に必要に応じて不活性ガス中で15
00〜3000℃に加熱して黒鉛化処理が行われている。これ
らの処理を行う加熱炉に於いては、繊維の処理を均一に
かつ安定して行うために炉内を所定の酸化性ガス濃度又
は不活性雰囲気(微酸素濃度)に保持することが必要で
ある。このため、加熱炉に於いては繊維トウの入口部及
び出口部から外気が侵入しないように防止策が講ずるこ
とが重要であり、種々のシール方法が提案されている。
(Prior Art) Generally, in order to produce carbon fibers, an organic polymer such as polyacrylonitrile, cellulose, petroleum-based pitch or coal-based pitch is spun and focused to obtain a fiber tow in an oxidizing atmosphere at 150 to 400. After carrying out flameproofing treatment or infusibilization treatment by heating to ℃, it is heated to 500 to 1500 ℃ in an inert gas to carry out carbonization treatment, and if necessary, in an inert gas.
It is heated to 00-3000 ℃ and graphitized. In a heating furnace that performs these treatments, it is necessary to maintain the inside of the furnace at a predetermined oxidizing gas concentration or an inert atmosphere (fine oxygen concentration) in order to perform the fiber treatment uniformly and stably. is there. Therefore, in a heating furnace, it is important to take preventive measures so that outside air does not enter from the inlet and outlet of the fiber tow, and various sealing methods have been proposed.

例えば炭化炉の場合、入口部及び出口部に種々の形状
の部材を設け、該部に不活性ガスを噴出させる方法(特
公昭47−26969、特開昭49−86635)、入口部及び出口部
の端部を液体中に浸漬する方法(特開昭48−24031)及
び入口部及び出口部に一対の中空な弾性部材、中空な剛
性部材、弾性ローラ又は剛性ローラあるいは表面が波型
の擦過板を設け、これらの部材又はローラで繊維トウを
加圧しながら滑動させる方法(特開昭48−14820、53−8
6896、57−117624)がある。
For example, in the case of a carbonization furnace, a member having various shapes is provided at the inlet and the outlet, and an inert gas is jetted to the portion (Japanese Patent Publication No. 47-26969, JP-A-49-86635), the inlet and the outlet. Method of immersing the end portion of liquid in a liquid (Japanese Patent Laid-Open No. 48-24031) and a pair of hollow elastic members at the inlet and outlet, a hollow rigid member, an elastic roller or a rigid roller, or a corrugated scraping surface And sliding the fiber tow while pressurizing the fiber tow with these members or rollers (JP-A-48-14820, 53-8).
6896, 57-117624).

(発明が解決しようとする問題点) ところが、ガスでシールする方法は装置が複雑にな
る、多量の不活性ガスが必要である、噴射ガス流によつ
て繊維が乱され単糸切れの原因となる等の欠点がある。
また液状でシールする方法は繊維トウにシール液体が付
着するので、入口部に用いる場合は炭化炉内に液が持ち
込まれて炉内の雰囲気が乱れる、出口部に用いる場合は
繊維トウの乾燥が必要となる欠点がある。また、物理的
に繊維トウを挟圧する方法は、繊維トウが部材やローラ
と接触するため毛羽立ちや単糸切れの原因となり、さら
に剛性体を用いる場合は繊維トウの両側部に必然的に繊
維トウの厚みの間隙が生じシール性が低下するという欠
点がある。
(Problems to be solved by the invention) However, the method of sealing with gas complicates the apparatus, requires a large amount of inert gas, and causes the fibers to be disturbed by the jet gas flow, resulting in breakage of single yarns. There are drawbacks such as
In addition, since the sealing liquid adheres to the fiber tow in the liquid sealing method, the liquid is brought into the carbonization furnace to disturb the atmosphere in the furnace when used at the inlet, and the fiber tow is dried when used at the outlet. There are some drawbacks needed. Further, the method of physically pinching the fiber tow causes fluffing and single yarn breakage because the fiber tow comes into contact with the member and the roller, and when a rigid body is used, the fiber tow is inevitably formed on both sides of the fiber tow. However, there is a drawback in that a gap of the thickness occurs and the sealing property is deteriorated.

(問題点を解決するための手段) そこで本発明者等は上記の問題点を解決すべく鋭意検
討を重ねた結果、加熱炉内への外気の侵入は、煙突効果
の逆の効果を利用して加熱炉の繊維トウの導入用開口及
び導出用開口の上端の位置を炉底の位置よりも低くする
ことにより防止され、入口部及び出口部のシール用ガス
の使用量が大幅に削減できることを見出し、この知見に
基づき本発明を完成した。
(Means for Solving Problems) Therefore, the inventors of the present invention have conducted extensive studies to solve the above problems, and as a result, the invasion of outside air into the heating furnace utilizes an effect opposite to the stack effect. This is prevented by lowering the positions of the upper and lower ends of the fiber tow introduction opening and the discharge opening of the heating furnace below the furnace bottom position, and it is possible to significantly reduce the amount of sealing gas used at the inlet and outlet. The present invention has been completed based on the findings.

すなわち、本発明の要旨は繊維トウを不融化処理又は
耐炎化処理を行つたのち炭化処理、さらに必要に応じて
黒鉛化処理を行うことにより炭化繊維を製造する方法に
於いて、前記処理工程の少なくとも一つの工程を、実質
的に水平な直胴部と、一端に繊維トウの導入用開口、他
端に導出用開口を有するトンネル炉であつて、両開口の
上端位置が前記直胴部の床の位置と同一乃至は下方に位
置するよう構成され、かつ、少くとも前記直胴部に雰囲
気ガスの導入管を具備した炉を用いて行うことを特徴と
する炭素繊維の製造方法に存する。
That is, the gist of the present invention is a method for producing a carbonized fiber by carrying out infusibilizing treatment or flameproofing treatment on the fiber tow, then carbonizing treatment, and further performing graphitizing treatment, if necessary. At least one step is a tunnel furnace having a substantially horizontal straight body part, an opening for introducing fiber tow at one end, and an opening for leading out at the other end, wherein the upper end positions of both openings are the straight body part. A carbon fiber manufacturing method is characterized in that it is carried out by using a furnace which is configured to be located at the same position as or below the position of the floor, and which is equipped with an atmosphere gas introduction pipe in at least the straight body part.

以下、本発明を詳細に説明する。先ず、本発明の出発
物質となる繊維トウは、例えばポリアクリロニトリル、
セルローズ、石油系ピツチ又は石炭系ピツチを周知の方
法で紡糸し、得られた繊維を500〜30,000本程度集束し
たものである。
Hereinafter, the present invention will be described in detail. First, the fiber tow as the starting material of the present invention is, for example, polyacrylonitrile,
It is prepared by spinning a cellulose, a petroleum-based pitch or a coal-based pitch by a known method and bundling about 500 to 30,000 fibers obtained.

また、繊維トウの加熱処理も周知の方法に従つて行わ
れる。即ち、繊維の耐炎化又は不融化処理は、繊維トウ
を例えば酸素、オゾン、空気、窒素酸化物、ハロゲン、
亜硫酸ガス等の酸化性雰囲気中で150〜400℃に加熱する
ことによつて行われる。また、繊維の炭化処理は、耐炎
化又は不融化した繊維トウを例えば窒素、アルゴン等の
不活性ガス雰囲気下で500〜1500℃に加熱することによ
つて行われる。さらに必要に応じて繊維の黒鉛化を行う
場合は、炭化した繊維トウを不活性ガス雰囲気下で1500
〜3000℃に加熱することによつて行われる。
The heat treatment of the fiber tow is also performed according to a known method. That is, the flame-proofing or infusibilizing treatment of the fiber is carried out by treating the fiber tow with, for example, oxygen, ozone, air, nitrogen oxides, halogen,
It is carried out by heating to 150 to 400 ° C. in an oxidizing atmosphere such as sulfurous acid gas. The carbonization treatment of the fibers is carried out by heating the flame-resistant or infusibilized fiber tow to 500 to 1500 ° C. under an atmosphere of an inert gas such as nitrogen or argon. When graphitizing the fiber as required, carbonize the fiber tow under an inert gas atmosphere at 1500
By heating to ~ 3000 ° C.

次に、本発明を図面に基づいて説明する。 Next, the present invention will be described based on the drawings.

第1図は本発明に用いる加熱炉の一例の説明図であ
る。図中1は繊維トウ、2はバー、4及び16は繊維トウ
導入用開口及び導出用開口、6、16はコンベア、11はト
ンネル炉の直胴部である。
FIG. 1 is an explanatory diagram of an example of a heating furnace used in the present invention. In the figure, 1 is a fiber tow, 2 is a bar, 4 and 16 are openings for introducing and leading out the fiber tow, 6 and 16 are conveyors, and 11 is a straight body part of a tunnel furnace.

トンネル炉は、水平に設置されている直胴部11の一端
に繊維トウ導入用開口4、他端に導出用開口16を有し、
両開口4及び16の上端位置5及び14が直胴部11の床9の
位置と同一乃至は床9の位置より下に、好ましくは0.5
〜10m低い位置となるよう構成される。導入管10、10′
は加熱用及び/又は雰囲気用ガスの供給用導管であり、
直胴部11の上面及び/又は側面に開口するよう設けられ
る。
The tunnel furnace has a fiber tow introduction opening 4 at one end of a straight body portion 11 installed horizontally and a lead-out opening 16 at the other end,
The upper end positions 5 and 14 of both openings 4 and 16 are the same as or below the position of the floor 9 of the straight body part 11, preferably 0.5.
Configured to be ~ 10m lower. Introductory pipe 10, 10 '
Is a conduit for supplying heating gas and / or atmosphere gas,
It is provided so as to open on the upper surface and / or the side surface of the straight body part 11.

コンベア6は、繊維トウ1をすだれ状に吊り下げたバ
ー2を繊維トウの導入用開口4からトンネル炉内に移動
するためのもので、開口4から傾斜筒7を経て直胴部11
の端部の間に架設される。
The conveyor 6 is for moving the bar 2 in which the fiber tow 1 is hung in a comb shape from the fiber tow introduction opening 4 into the tunnel furnace.
Erected between the ends of.

ガイドレール12は、トンネル炉の一端より他端へバー
2を移動させるためのもので、直胴部11の上部に張架さ
れる。
The guide rail 12 is for moving the bar 2 from one end of the tunnel furnace to the other end, and is stretched over the straight body portion 11.

コンベア19は、バー2を繊維トウ脱離部Bから繊維ト
ウ載置部Aへ移送するためのもので、トンネル炉のシュ
ート13の出口17と開口4の間のトンネル炉外に架設され
る。
The conveyor 19 is for transferring the bar 2 from the fiber tow desorption section B to the fiber tow placing section A, and is installed outside the tunnel furnace between the outlet 17 of the chute 13 of the tunnel furnace and the opening 4.

バー2としては、周知のもの例えば横断面が円形又は
星形をした棒状のものも使用できるが、水平切断面の周
縁形状が凹凸状乃至は蛇行状をなし、横断面の形状が円
形、楕円形、多角形、星形等のものを使用するのが好ま
しい。このような構造のバーを用いる場合は、繊維トウ
のすだれ状の表面が平面とならず凹凸状となる。従つ
て、炉内へ供給した気体及び加熱により発生したガスは
生成したすき間から矢印の方向に流通するので、均質な
加熱処理を行うことができる。
As the bar 2, well-known ones, for example, rod-shaped ones having a circular cross section or a star shape can be used, but the peripheral shape of the horizontal cut surface is uneven or meandering, and the cross section has a circular or elliptical shape. It is preferable to use shapes, polygons, stars and the like. In the case of using the bar having such a structure, the interdigital surface of the fiber tow becomes uneven rather than flat. Therefore, the gas supplied into the furnace and the gas generated by heating flow in the direction of the arrow from the generated gap, so that a uniform heat treatment can be performed.

(作 用) 次に、このように構成された加熱炉を用いて繊維トウ
の加熱処理を行う方法を説明する。
(Operation) Next, a method of heating the fiber tow by using the heating furnace configured as described above will be described.

第1図に於いて、トンネル炉は、導入管10、10′……
より供給され、開口4及び16より排出される雰囲気ガス
により所定の雰囲気ガス濃度に保持され、又、同ガス及
び/又は他の熱源により所定の温度に保持される。コン
ベア6及び19は矢印の方向に駆動される。繊維トウ1
は、水平方向に複数本(例えば20〜500本)並んだ状態
で繊維トウ載置部Aへ供給され、該部に於いて、コンベ
ア19で搬送されてきたバー2で下方からすくわれるよう
にして折りたたまれ、バー2にすだれ状に吊り下げられ
る。繊維トウ1を吊り下げたバー2は、コンベア19とコ
ンベア6との交差点3でコンベア19からコンベア6へ移
動され、直胴部11の端部に於いてプツシヤー8によりコ
ンベア6からガイドレール12へ移動される。ガイドレー
ル12上では、プツシヤー8の1動作毎にバー2が1個分
ずつ右方向へ移動される。繊維トウ脱離部Bへ到達した
バー2は、ローラ15の駆動により繊維トウ1が順次引き
上げられる。繊維トウ1が脱離されたバー2は、プツシ
ヤー8の作動によりシユート13へ落され、該シユートの
出口17に於いてコンベア19のバー係止具18に係止され、
繊維トウ載置部Aの方向へ移動される。
In Fig. 1, the tunnel furnace is shown as an inlet pipe 10, 10 '...
The ambient gas supplied from the openings 4 and 16 is maintained at a predetermined ambient gas concentration, and is maintained at a predetermined temperature by the ambient gas and / or another heat source. The conveyors 6 and 19 are driven in the direction of the arrow. Fiber tow 1
Is fed to the fiber tow placing section A in a state where a plurality of pieces (for example, 20 to 500 pieces) are aligned in the horizontal direction, and at that portion, the bar 2 conveyed by the conveyor 19 is scooped from below. It is folded up and hung on the bar 2 in a blind shape. The bar 2 on which the fiber tow 1 is hung is moved from the conveyor 19 to the conveyor 6 at the intersection 3 of the conveyor 19 and the conveyor 6, and at the end of the straight body part 11 from the conveyor 6 to the guide rail 12 by the pusher 8. Be moved. On the guide rail 12, one bar 2 is moved rightward for each movement of the pusher 8. When the bar 2 reaches the fiber tow detachment section B, the fiber tow 1 is sequentially pulled up by driving the roller 15. The bar 2 from which the fiber tow 1 is detached is dropped into the shout 13 by the operation of the pusher 8 and is locked at the bar lock 18 of the conveyor 19 at the exit 17 of the shout.
It is moved in the direction of the fiber tow rest A.

なお、第1図に於いて、プツシヤー8に代えて爪を設
けたローラを用い、該爪にてバー2をガイドレール12上
へ移動させることができる。また、ガイドレール12に代
えて、コンベア6を直胴部11迄延長したものを用いるこ
とができる。この場合はプツシヤー8は不要となる。
In FIG. 1, a roller provided with a claw instead of the pusher 8 can be used to move the bar 2 onto the guide rail 12 by the claw. Further, instead of the guide rail 12, it is possible to use one in which the conveyor 6 is extended to the straight body portion 11. In this case, the pusher 8 becomes unnecessary.

次に、本発明に用いる加熱炉の他の例を第2図に基づ
いて説明する。第2図は両開口4及び16がそれぞれ導入
部傾斜筒7及び導出部傾斜筒20の下端で開口し、その形
状及び開口上端の位置5及び14等を実質的に同一形状つ
まりトンネル炉の両端部を対称形にした例であり、逆煙
突効果が一層効果的に発現される。第2図中第1図と同
一番号及び記号は第1図と同一の意義を有する。
Next, another example of the heating furnace used in the present invention will be described with reference to FIG. FIG. 2 shows that both openings 4 and 16 open at the lower ends of the introductory part inclination cylinder 7 and the outlet part inclination cylinder 20, respectively, and their shapes and positions 5 and 14 of the opening upper end are substantially the same, that is, both ends of the tunnel furnace This is an example in which the parts are made symmetrical, and the reverse chimney effect is more effectively exhibited. In FIG. 2, the same numbers and symbols as in FIG. 1 have the same meanings as in FIG.

第2図に於いて、コンベア21は繊維トウ1をすだれ状
に吊り下げたバー2をトンネル炉内から取り出すための
もので、直胴部11の端部から傾斜筒20を経て開口16の間
に架設される。
In FIG. 2, a conveyor 21 is for taking out the bar 2 in which the fiber tow 1 is hung in a comb shape from the inside of the tunnel furnace, and from the end of the straight body part 11 to the opening 16 via the inclined cylinder 20. Erected in.

第2図に示す加熱炉に於いては、第1図の場合と同様
の方法でガイドレール12上を移動してきたバー2は、コ
ンベア21へ載せられて繊維トウ脱離部Bへ送られる。コ
ンベア21のスピードはコンベア6と同一乃至は数倍の速
さ(すなわち、繊維トウが傾斜筒20内をほゞ直線状で引
き出されるようになるまでの速さ)である。繊維トウ脱
離部Bへ到達したバー2は、ローラ22の駆動により繊維
トウ1が順次引上げられ、次いで、コンベア19との交差
点23に於いて、下方から上昇するコンベア19のバー係止
具18に係止され、繊維トウ載置部Aの方向へ移動され
る。
In the heating furnace shown in FIG. 2, the bar 2 that has moved on the guide rail 12 in the same manner as in the case of FIG. 1 is placed on the conveyor 21 and sent to the fiber tow detachment section B. The speed of the conveyor 21 is the same as or several times as fast as the conveyor 6 (that is, the speed at which the fiber tow is pulled out in the inclined cylinder 20 in a substantially straight line shape). The bar 2 that has reached the fiber tow detachment section B is sequentially pulled up by the drive of the roller 22, and then, at the intersection 23 with the conveyor 19, the bar locking member 18 of the conveyor 19 that rises from the lower side. And is moved in the direction of the fiber tow placing portion A.

なお、第2図に於いて、プツシヤー8に代えて爪を設
けたローラを用い、該爪にてバー2をガイドレール12へ
移動させることができる。また、ガイドレール12に代え
て、コンベア6及び21を直胴部11迄延長し、かつ一体化
したコンベアを用いることができる。この場合はプツシ
ヤー8は不要となる。
In FIG. 2, a roller provided with a claw instead of the pusher 8 can be used to move the bar 2 to the guide rail 12 by the claw. Further, instead of the guide rail 12, it is possible to use a conveyor in which the conveyors 6 and 21 are extended to the straight body portion 11 and integrated. In this case, the pusher 8 becomes unnecessary.

更に、本発明に用いる加熱炉の他の例を第3図に基づ
いて説明する。
Further, another example of the heating furnace used in the present invention will be described with reference to FIG.

第3図中、第1図と同一の番号及び記号は第1図と同
一の意義を有する。第3図に於いて、加熱炉は、導入管
10,10′,10″より供給され、開口4及び16より排出され
る雰囲気ガスにより所定の雰囲気ガス濃度に保持され、
又同ガス及び/又は他の熱源により所定の温度に保持さ
れる。コンベア19及び25は矢印の方向に駆動される。繊
維トウ1は、水平方向に複数本(例えば20〜500本)に
並んだ状態で開口4より加熱炉内へ連続的に供給され、
繊維トウ載置部Aに於いて、コンベア19で搬送されてき
たバー2で下方からすくわれるようにして折りたたま
れ、バー2にす6れ状に吊り下げられる。繊維トウ1を
吊り下げたバー2は、転動装置24によりコンベア25上へ
載置され、炉内を右方向へ移動される。繊維トウ脱離部
Bへ到達したバー2は、ローラ15の駆動により繊維トウ
1が順次引き上げられた後、下方より上昇するコンベア
19のバー係止具18に係止され、繊維トウ載置部Aの方向
へ移動される。バー2から脱離された繊維トウ1は開口
16より連続的に取出される。
In FIG. 3, the same numbers and symbols as in FIG. 1 have the same meanings as in FIG. In FIG. 3, the heating furnace is an inlet pipe.
The atmosphere gas supplied from 10, 10 ', 10 "and discharged from the openings 4 and 16 maintains a predetermined atmosphere gas concentration,
Further, the gas and / or another heat source keeps the temperature at a predetermined level. The conveyors 19 and 25 are driven in the direction of the arrow. The fiber tow 1 is continuously fed into the heating furnace through the opening 4 in a state where a plurality of fibers (for example, 20 to 500) are arranged in the horizontal direction,
In the fiber tow placement section A, the bar 2 conveyed by the conveyor 19 is folded so as to be scooped from below and is hung on the bar 2 in a comb shape. The bar 2 on which the fiber tow 1 is suspended is placed on the conveyor 25 by the rolling device 24 and moved rightward in the furnace. The bar 2 that has reached the fiber tow detachment section B is moved up from below after the fiber tow 1 is sequentially pulled up by the drive of the roller 15.
It is locked by the bar locking tool 18 of 19 and moved toward the fiber tow mounting portion A. Fiber tow 1 detached from bar 2 is open
It is taken out continuously from 16.

なお、第3図の装置に於いて、雰囲気ガスは、加熱炉
の側面から供給することもできる。また、転動装置24の
代りに、第1図に示したと同様のプツシヤー又は爪を設
けたローラを用いることができる。さらに、プツシヤー
又は爪を設けたローラを用いる場合は、コンベア25の代
りに第1図に示したと同様のガイドレールを用いること
ができる。
In the apparatus of FIG. 3, the atmospheric gas can be supplied from the side of the heating furnace. Further, instead of the rolling device 24, a roller provided with a pusher or a claw similar to that shown in FIG. 1 can be used. Further, when using a roller provided with a pusher or a claw, the guide rail similar to that shown in FIG. 1 can be used instead of the conveyor 25.

更に、本発明に用いる加熱炉の他の例を第4図〜第7
図に基づいて説明する。第4図〜第7図は繊維トウ導入
用開口及び導出用開口の構成のみを示すための加熱炉の
概略説明図であり、図中第1図と同一の番号は第1図と
同一の意義を有し、他の構成部分は全て省略してある。
Furthermore, other examples of the heating furnace used in the present invention are shown in FIGS.
It will be described with reference to the drawings. 4 to 7 are schematic explanatory views of the heating furnace for showing only the configurations of the fiber tow introduction opening and the discharge opening, and the same numbers as in FIG. 1 have the same meanings as in FIG. , And all other components are omitted.

第4図は、開口4及び16をL形筒を介して直胴部11に
設けた場合である。第5図は、開口4及び16を直筒を介
して直胴部11に設けた場合である。第6図は、第2図に
示す如き加熱炉であが各傾斜筒に設けられた導入用及び
導出用の開口4及び16をいずれも実質的に水平としたも
のである。この様に導入部又は導出部に傾斜筒を使用す
る場合はその開口を実質的に水平とすることにより横風
等の外気の気流次第では傾斜筒の下層に発生するかも知
れない外気の上昇流をより良く防止できて好適であり、
少くとも第7図の如く外気の浸入が起り易い導入部傾斜
筒の開口のみは実質的に水平とすることが望ましい。
FIG. 4 shows the case where the openings 4 and 16 are provided in the straight body portion 11 via the L-shaped tube. FIG. 5 shows a case where the openings 4 and 16 are provided in the straight body portion 11 via a straight cylinder. FIG. 6 shows the heating furnace as shown in FIG. 2 in which the inlet and outlet openings 4 and 16 provided in each inclined cylinder are substantially horizontal. In this way, when an inclined cylinder is used for the inlet or outlet, by making the opening substantially horizontal, the upward flow of outside air that may occur in the lower layer of the inclined cylinder depending on the airflow of outside air such as crosswind. It can prevent better and is suitable,
As shown in FIG. 7, it is desirable that at least the opening of the introduction portion inclined cylinder where the outside air is likely to enter is substantially horizontal.

又、傾斜筒の垂直方向に対する傾斜角が余りに大きい
(水平に近くなる)と外気の浸入が生じ易くなるので一
般には60度以下、より好ましくは45度以下とすべきであ
る。なお、傾斜筒を使用するいずれの場合も筒内を流出
する炉内雰囲気ガスの流れが筒の上層部のみに偏らない
様に適宜の位置及び適宜形状の気流案内板を設けること
も推奨される。
Further, if the inclination angle of the inclined cylinder with respect to the vertical direction is too large (close to horizontal), infiltration of outside air is likely to occur, so it should generally be 60 degrees or less, more preferably 45 degrees or less. In any case where a tilted cylinder is used, it is also recommended to provide an air flow guide plate with an appropriate position and shape so that the flow of the furnace atmosphere gas flowing out of the cylinder is not biased only to the upper layer of the cylinder. .

上述の導入部及び導出部の形状は必ずしも同一である
必要はなく各形状を組合せて採用して良いが、前述した
様に、導入部の方が外気の浸入をより良く防止し得る形
状に選択するのが好ましい。
The shapes of the above-mentioned introduction part and the derivation part do not necessarily have to be the same, and it is possible to adopt a combination of each shape, but as mentioned above, the introduction part is selected to a shape that can better prevent the infiltration of outside air. Preferably.

以上、詳述した通り本発明で用いる加熱炉の形式は種
々の変形が可能であるが、いずれの場合にも導入用開口
及び導出用開口の上端がいずれも直胴部の床の位置以
下、より好ましくは、0.5〜10mより下方に設定されるこ
と及び少くとも直胴部でその上方部及び/又は側方部に
雰囲気ガスの導入管が具備されていることが重要であ
る。即ち導入された雰囲気ガスは外気よりはるかに高温
であるので直胴部の床以下に設定された繊維の導入用及
び導出用開口から排出されることによりそれら開口が相
当大きい場合でも逆煙突効果によつて外気の炉内への浸
入を自然に防止できることとなる。
As described above, the type of the heating furnace used in the present invention can be variously modified as described in detail, but in any case, the upper ends of the introduction opening and the extraction opening are both below the floor position of the straight body part, More preferably, it is important that it is set below 0.5 to 10 m and that at least a straight body portion is provided with an atmospheric gas introduction pipe in an upper portion and / or a side portion thereof. That is, since the introduced atmospheric gas is much hotter than the outside air, the reverse chimney effect can be obtained even if those openings are considerably large by being discharged from the fiber introduction and discharge openings set below the floor of the straight body part. Therefore, the invasion of outside air into the furnace can be naturally prevented.

なお、本発明に用いる加熱炉は任意形式を2基連接し
て不融化炉もしくは耐炎化炉及び炭化炉として構成する
こともでき、又全く別形式の耐炎化炉もしくは不融化炉
に炭化炉として接続することもできる。いずれの場合も
連接点で各炉の雰囲気ガスが他炉へ混入しない様に適切
な排気手段を考慮すべきである。
The heating furnace used in the present invention may be constructed by connecting two arbitrary types as an infusibilizing furnace or a flameproofing furnace and a carbonizing furnace, or by using a completely different type flameproofing furnace or infusibilizing furnace as a carbonizing furnace. You can also connect. In any case, appropriate exhaust means should be considered so that the atmosphere gas of each furnace does not mix with other furnaces at the contact points.

以上、繊維トウをバーに吊り下げた状態で加熱処理を
行う場合について説明したが、本発明は繊維トウをケン
スに入れた状態で加熱炉内を移動させる方法や繊維トウ
を張力をかけた状態で加熱炉内を移動させる方法によつ
て実施することもできる。
As described above, the case where the heat treatment is performed while the fiber tow is hung on the bar has been described, but the present invention is a method in which the fiber tow is moved in the heating furnace in a can and a state in which the fiber tow is tensioned. It can also be carried out by a method of moving the inside of the heating furnace.

(発明の効果) 以上説明したように、本発明では繊維トウの加熱処理
を行うに際し、加熱炉における繊維トウの導入用開口と
導出用開口に特別のシール機構を設けなくとも、その上
端の位置を加熱炉の床の位置と同一乃至は下方に位置す
るように構成し、かつ、少くとも炉の直胴部に雰囲気ガ
スを導入することにより、加熱炉内への外気の侵入を効
果的に阻止することができる。
(Effects of the Invention) As described above, in the present invention, when the heat treatment of the fiber tow is performed, the position of the upper end of the fiber tow is not required to be provided in the heating furnace even if a special sealing mechanism is not provided. Is configured to be located at the same position as or below the floor of the heating furnace, and by introducing an atmosphere gas into at least the straight body part of the furnace, it is possible to effectively prevent outside air from entering the heating furnace. Can be stopped.

従つて本発明に於いては、繊維の炉内への入出口条件
(形状、大きさ、量等)に余り制約を受けないので典型
的にはバーにすだれ状に吊り下げる方式やケンス装入方
式で処理できることは勿論、ロール方式にしても大量の
繊維に対し、常時所定の雰囲気ガス組成を保持できる結
果、均質な不融化、耐炎化、炭化、黒鉛化等の処理を容
易に行うことができる。特に炭化処理及び黒鉛化処理の
際雰囲気ガス中の酸素濃度を10ppm以下にすることがで
きるので、高品質の繊維を得ることができる等炭素繊維
の製造法として有用である。
Therefore, in the present invention, since there is not much restriction on the conditions (shape, size, amount, etc.) of entering and exiting the fiber into the furnace, it is typically a method of hanging in a comb shape on a bar or a can charging. Not only can it be processed by a method, but even if it is a roll method, a large amount of fibers can always maintain a predetermined atmospheric gas composition, and as a result, it is possible to easily carry out uniform infusibilization, flame resistance, carbonization, graphitization, etc. it can. In particular, since the oxygen concentration in the atmosphere gas can be set to 10 ppm or less during the carbonization treatment and the graphitization treatment, it is useful as a method for producing carbon fibers such that high quality fibers can be obtained.

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

第1図〜第3図はそれぞれ本発明に用いる加熱炉の一例
の説明図、であり第4図〜第7図は更にこれら加熱炉に
おける繊維トウの導入部及び導出部の他の例を主として
示す為の概略説明図、である。 1:繊維トウ 4:繊維トウ導入用開口 5:繊維トウ導入用開口の上端 7:繊維トウ導入部傾斜筒 9:トンネル炉の床 10、10′、10″:雰囲気ガス導入管 11:トンネル炉の直胴部 14:繊維トウ導出用開口の上端 16:繊維トウ導出用開口 20:繊維トウ導出部傾斜筒 A:繊維トウ載置部 B:繊維トウ脱離部
1 to 3 are explanatory views of an example of a heating furnace used in the present invention, and FIGS. 4 to 7 are mainly other examples of the introduction part and the extraction part of the fiber tow in these heating furnaces. It is a schematic explanatory drawing for showing. 1: Fiber tow 4: Fiber tow introduction opening 5: Fiber tow introduction opening 7: Fiber tow introduction part inclined cylinder 9: Tunnel furnace floor 10, 10 ′, 10 ″: Atmosphere gas introduction pipe 11: Tunnel furnace Straight body part 14: Upper end of fiber tow lead-out opening 16: Fiber tow lead-out opening 20: Fiber tow lead-out part Inclined cylinder A: Fiber tow rest part B: Fiber tow release part

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 実開 昭54−82182(JP,U) 特公 昭40−2709(JP,B1) 特公 昭60−30362(JP,B2) ─────────────────────────────────────────────────── ─── Continuation of the front page (56) Bibliographic references Sho 54-82182 (JP, U) Japanese Patent Sho 40-2709 (JP, B1) Japanese Official Sho 60-30362 (JP, B2)

Claims (7)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】繊維トウを不融化処理又は耐炎化処理を行
つたのち炭化処理、さらに必要に応じて黒鉛化処理を行
うことにより炭素繊維を製造する方法に於いて、前記処
理工程の少なくとも一つの工程を、実質的に水平な直胴
部と、一端に繊維トウの導入用開口、他端に導出用開口
を有するトンネル炉であつて、両開口の上端位置が前記
直胴部の床の位置と同一乃至は下方に位置するよう構成
され、かつ、少くとも前記直胴部部に雰囲気ガスの導入
管を具備した炉を用いて行うことを特徴とする炭素繊維
の製法。
1. A method for producing a carbon fiber by subjecting a fiber tow to an infusibilizing treatment or a flameproofing treatment, followed by a carbonization treatment and, if necessary, a graphitization treatment, wherein at least one of the treatment steps is performed. One of the steps is a tunnel furnace having a substantially horizontal straight body part, an opening for introducing fiber tow at one end, and an opening for leading out at the other end, the upper end positions of both openings being the floor of the straight body part. A method for producing carbon fiber, which is characterized in that it is arranged at the same position as or below the position, and is carried out using a furnace equipped with an atmosphere gas introduction pipe at least in the straight body part.
【請求項2】前記繊維トウがピツチ繊維トウである特許
請求の範囲第(1)項記載の炭素繊維の製法。
2. The method for producing a carbon fiber according to claim 1, wherein the fiber tow is a pitch fiber tow.
【請求項3】前記繊維トウがピツチ繊維トウを不融化処
理したものである特許請求の範囲第(1)項記載の炭素
繊維の製法。
3. The method for producing a carbon fiber according to claim 1, wherein the fiber tow is an infusibilized Pitch fiber tow.
【請求項4】前記導入用開口及び前記導出用開口がそれ
ぞれ前記直胴部に接続した導入部傾斜筒及び導出部傾斜
筒の下端で開口していることを特徴とする特許請求の範
囲第(1)項乃至第(3)項のいずれかに記載の炭素繊
維の製法。
4. The introductory opening and the outgoing opening are opened at the lower ends of the introductory portion inclination tube and the outflowing portion inclination tube, respectively, which are connected to the straight body portion. The method for producing a carbon fiber according to any one of 1) to (3).
【請求項5】前記導入用開口と前記導出用開口の中、少
くとも導入用開口が実質的に水平に開口していることを
特徴とする特許請求の範囲第(4)項記載の炭素繊維の
製法。
5. The carbon fiber according to claim 4, wherein at least the introduction opening is substantially horizontal among the introduction opening and the extraction opening. Manufacturing method.
【請求項6】前記導入用開口と前記導出口開口のいずれ
もが実質的に水平に開口していることを特徴とする特許
請求の範囲第(5)項記載の炭素繊維の製法。
6. The method for producing carbon fiber according to claim 5, wherein both the introduction opening and the outlet opening are opened substantially horizontally.
【請求項7】前記導入部傾斜筒及び前記導出部傾斜筒が
垂直方向に対し60度以下の角度で傾斜していることを特
徴とする特許請求の範囲第(4)項記載の炭素繊維の製
法。
7. The carbon fiber according to claim 4, wherein the introductory-portion slanting cylinder and the lead-out slanting cylinder are inclined at an angle of 60 degrees or less with respect to a vertical direction. Manufacturing method.
JP61283551A 1986-11-28 1986-11-28 Carbon fiber manufacturing method Expired - Lifetime JP2507367B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61283551A JP2507367B2 (en) 1986-11-28 1986-11-28 Carbon fiber manufacturing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61283551A JP2507367B2 (en) 1986-11-28 1986-11-28 Carbon fiber manufacturing method

Publications (2)

Publication Number Publication Date
JPS63135521A JPS63135521A (en) 1988-06-07
JP2507367B2 true JP2507367B2 (en) 1996-06-12

Family

ID=17666988

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61283551A Expired - Lifetime JP2507367B2 (en) 1986-11-28 1986-11-28 Carbon fiber manufacturing method

Country Status (1)

Country Link
JP (1) JP2507367B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN119615423B (en) * 2024-12-23 2025-07-18 苏州斯泰特智能装备有限公司 A special production equipment for carbon fiber spinning composite material

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5482182U (en) * 1977-11-19 1979-06-11
JPS6030362A (en) * 1983-07-28 1985-02-15 Matsushita Graphic Commun Syst Inc Trans-thermo recording system

Also Published As

Publication number Publication date
JPS63135521A (en) 1988-06-07

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