JPS6311448B2 - - Google Patents
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- Publication number
- JPS6311448B2 JPS6311448B2 JP54114509A JP11450979A JPS6311448B2 JP S6311448 B2 JPS6311448 B2 JP S6311448B2 JP 54114509 A JP54114509 A JP 54114509A JP 11450979 A JP11450979 A JP 11450979A JP S6311448 B2 JPS6311448 B2 JP S6311448B2
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- Prior art keywords
- heating element
- graphite
- carbon
- inert gas
- pipe
- Prior art date
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- Inorganic Fibers (AREA)
- Resistance Heating (AREA)
- Carbon And Carbon Compounds (AREA)
- Furnace Details (AREA)
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、炭素繊維を連続的に生産効率良く製
造するための炭素繊維の製造装置に関するもので
ある。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a carbon fiber manufacturing apparatus for continuously manufacturing carbon fibers with high production efficiency.
[従来の技術]
通常、炭素繊維を製造するには、ポリアクリロ
ニトリル繊維、再生セルローズ繊維、フエノール
系繊維、ピツチ系繊維等の有機重合体を先ず空気
又は他の酸化性ガス雰囲気中にて200〜300℃で耐
炎化し、次いでこれを窒素、アルゴン等の不活性
ガス雰囲気中にて800〜2000℃で炭化して製造さ
れる。又、更に1500〜3000℃で黒鉛化を行ない、
ヤング率が一段と高い炭素繊維を製造することも
行なわれる。[Prior Art] Normally, in order to produce carbon fibers, organic polymers such as polyacrylonitrile fibers, regenerated cellulose fibers, phenolic fibers, and pitch fibers are first heated to 200 to It is produced by making it flameproof at 300°C and then carbonizing it at 800-2000°C in an inert gas atmosphere such as nitrogen or argon. Furthermore, graphitization is performed at 1500 to 3000℃,
Carbon fibers with even higher Young's moduli are also produced.
しかるに、上記の炭化及び黒鉛化工程における
糸条処理温度は非常に高く、特に、処理温度1500
〜3000℃が要求される黒鉛化工程の高温加熱装置
では、材料の高温に於ける熱的、化学的諸特性お
よび後述する電気的特性上の制約から、高温加熱
装置の発熱体としてカーボン或はグラフアイト材
を筒状に構成したものを用い、その内部に糸条を
通過させて高温処理することが多い。この場合、
上記のカーボン或はグラフアイト材からなる発熱
体は高温下に於ける酸化雰囲気中での酸化反応が
著しく、極めて短時間で減耗劣化して使用に耐え
得なくなることがよく知られており、その対策と
して、高温加熱装置内に窒素、アルゴン等の不活
性ガスを導入して大気圧よりも僅かに高い内圧を
維持せしめ、発熱体の内外表面の雰囲気制御を行
つている。 However, the yarn treatment temperature in the above carbonization and graphitization steps is extremely high, especially at a treatment temperature of 1500
In the high-temperature heating equipment used in the graphitization process, which requires a temperature of ~3000°C, carbon or A cylindrical graphite material is often used, and a thread is passed through the cylindrical material to undergo high-temperature treatment. in this case,
It is well known that the above-mentioned heating elements made of carbon or graphite materials undergo a significant oxidation reaction in an oxidizing atmosphere at high temperatures, and wear out and deteriorate in an extremely short period of time, making them unusable. As a countermeasure, an inert gas such as nitrogen or argon is introduced into the high-temperature heating device to maintain an internal pressure slightly higher than atmospheric pressure, thereby controlling the atmosphere on the inner and outer surfaces of the heating element.
一方、上記のカーボン或はグラフアイトよりな
る発熱体を高温に於いて効率よく安全にその特性
を発揮せしめるために、筒状に構成された当該発
熱体の外側周辺にカーボンあるいはグラフアイト
の粒子又は粉末を充填し、高温発熱体の中間支持
材兼断熱材としての機能を果たすような構成がと
られる。更に上記の高温加熱装置の加熱手段とし
ては、一般にタンマン型式又は高周波誘導方式に
よる発熱体自体の電流によるジユール発熱作用が
利用されている。 On the other hand, in order to make the heating element made of carbon or graphite exhibit its characteristics efficiently and safely at high temperatures, carbon or graphite particles or The structure is such that it is filled with powder and functions as an intermediate support material and a heat insulating material for the high-temperature heating element. Further, as the heating means of the above-mentioned high-temperature heating device, a Joule heating effect using the electric current of the heating element itself is generally used, such as a Tammann type or a high frequency induction type.
次に、上記従来の装置を図面を用いて、より具
体的に説明する。 Next, the above-mentioned conventional device will be explained in more detail with reference to the drawings.
第1図は、上述の炭素繊維を製造するために炭
化または黒鉛化工程に従来一般的に用いられてい
るタンマン型式の炉の一例を示す概略横断面図で
ある。第1図に示す装置を特に黒鉛化炉にみたて
て説明すれば、炭化系1をニツプローラ2によつ
て黒鉛化炉10にその一端から連続的に導入し、
黒鉛化炉10内で黒鉛化処理した後、ニツプロー
ラ3によつて他端から黒鉛化繊維1′として連続
的に導出できるようになつている。本炉10にお
いて、円筒状に構成されたグラフアイト発熱体4
は中間支持材兼断熱材として炉内に充填されたグ
ラフアイトパウダ5によつて断熱支持され、当該
グラフアイト発熱体4は低電圧大電流の電源を水
冷電極6に接続し直接通電によるジユール発熱に
よつて、温度2500℃〜3000℃の高温が得られるよ
うになつている。黒鉛化炉10内は、あらかじめ
窒素ガスによつて置換えされており、運転時にお
いても、黒鉛化炉10に設けられた窒素ガスの流
入口7から連続的に窒素ガスをグラフアイト発熱
体4内に通気させて流出口8から流出させる構造
を成している。 FIG. 1 is a schematic cross-sectional view showing an example of a Tanmann type furnace conventionally commonly used in a carbonization or graphitization process to produce the above-mentioned carbon fibers. To explain the apparatus shown in FIG. 1 in particular as a graphitization furnace, a carbonized system 1 is continuously introduced into a graphitization furnace 10 from one end by a nip roller 2,
After being graphitized in the graphitization furnace 10, it can be continuously drawn out from the other end by a nip roller 3 as a graphitized fiber 1'. In the main furnace 10, a graphite heating element 4 configured in a cylindrical shape
is thermally supported by graphite powder 5 filled in the furnace as an intermediate support and heat insulating material, and the graphite heating element 4 generates heat by connecting a low-voltage, high-current power source to the water-cooled electrode 6 and directly energizing it. It is now possible to obtain high temperatures of 2500°C to 3000°C. The inside of the graphitization furnace 10 is replaced with nitrogen gas in advance, and even during operation, nitrogen gas is continuously supplied into the graphite heating element 4 from the nitrogen gas inlet 7 provided in the graphitization furnace 10. It has a structure in which the water is ventilated and flows out from the outflow port 8.
[発明が解決しようとする問題点]
しかるに上述した従来の高温加熱装置は、前記
した種々の工夫にも拘らず、カーボン或はグラフ
アイトからなる発熱体自体の温度が1500〜3000℃
と非常に高いために加熱装置内の残存酸素との反
応あるいは炭素質の蒸発等が起り、極めて短時間
で減耗、劣化し、頻繁な発熱体交換作業を余儀な
くされることにある。又上記の蒸発現象は、雰囲
気温度が2000℃を超えると、急速に激しくなると
考えられ、特に発熱体の外周表面の減耗が著しか
つた。しかるに本発明の目的は、従来技術に於け
る上記の問題を大幅に克服可能ならしめる高温加
熱装置を提供することにある。[Problems to be Solved by the Invention] However, in the above-mentioned conventional high-temperature heating device, despite the various devices described above, the temperature of the heating element itself made of carbon or graphite is 1500 to 3000°C.
Because of this extremely high temperature, a reaction with the residual oxygen in the heating device or evaporation of carbonaceous material may occur, resulting in wear and tear in an extremely short period of time, making it necessary to frequently replace the heating element. Further, the above-mentioned evaporation phenomenon is thought to rapidly become more intense when the ambient temperature exceeds 2000°C, and the wear on the outer circumferential surface of the heating element is particularly significant. SUMMARY OF THE INVENTION However, it is an object of the present invention to provide a high temperature heating device which makes it possible to largely overcome the above-mentioned problems of the prior art.
[問題点を解決するための手段]
本発明は、グラフアイトあるいはカーボンから
なる筒状の発熱体と、該発熱体の両端に設けた電
極と、該発熱体の外周に設けた断熱材と、該発熱
体の片側に設けられ筒内に連通した不活性ガス流
入口と、該発熱体の他の片側に設けられ筒内に連
通した不活性ガス排出口とからなる炭素繊維の製
造装置において、前記断熱材と発熱体との間に、
内径が該発熱体の外形より大で、かつ、グラフア
イトあるいはカーボンからなるパイプを、該パイ
プが鞘で該発熱体が芯となる位置に設け、該パイ
プと発熱体との間に形成された間隙部の両側を開
口せしめ、該開口部の片側を前記不活性ガス流入
口に、該開口部の他の片側を前記不活性ガス排出
口にそれぞれ連通せしめたことを特徴とする炭素
繊維の製造装置を要旨とするものである。[Means for Solving the Problems] The present invention includes a cylindrical heating element made of graphite or carbon, electrodes provided at both ends of the heating element, a heat insulating material provided around the outer periphery of the heating element, A carbon fiber manufacturing apparatus comprising an inert gas inlet provided on one side of the heating element and communicating with the inside of the cylinder, and an inert gas outlet provided on the other side of the heating element and communicating with the inside of the cylinder, between the heat insulating material and the heating element,
A pipe having an inner diameter larger than the outer diameter of the heating element and made of graphite or carbon is provided at a position where the pipe is a sheath and the heating element is the core, and is formed between the pipe and the heating element. Production of carbon fiber characterized in that both sides of the gap are open, one side of the opening communicates with the inert gas inlet, and the other side of the opening communicates with the inert gas outlet. The gist is the device.
次に、本発明の装置を、図面を参照しながら説
明する。 Next, the apparatus of the present invention will be explained with reference to the drawings.
第3図は、第1図に示した従来の黒鉛化炉10
を本発明にしたがつて改造した黒鉛化炉20の概
略横断面図を、第4図は、本黒鉛化炉20中央部
の概略縦断面図を示す。 FIG. 3 shows the conventional graphitization furnace 10 shown in FIG.
FIG. 4 shows a schematic cross-sectional view of a graphitizing furnace 20 modified according to the present invention, and FIG. 4 shows a schematic vertical cross-sectional view of the central part of the graphitizing furnace 20.
本黒鉛化炉20のグラフアイト発熱体4には、
その外周部軸方向に沿つて6本のクリアランス部
をなす外周部溝22が切つてあり、溝を切り残し
た6本の凸部23で黒鉛材あるいはグラフアイト
フエルトからなるパイプ21に接し、該パイプ2
1が鞘でグラフアイト発熱体4が芯となる位置に
配置されて支持され、その外周にカーボンパウダ
5が詰めてある。なお、パイプ21の内径がグラ
フアイト発熱体4の外形より大きいのでクリアラ
ンス22が形成される。このクリアランス22
は、図示したごとく両側が開口されて、片側が窒
素流入口7に、また、他の片側は、窒素排出口8
にそれぞれ連通している。 The graphite heating element 4 of the present graphitization furnace 20 includes:
Six outer circumferential grooves 22 forming clearance parts are cut along the axial direction of the outer circumference, and the six protrusions 23 with the grooves left in contact with the pipe 21 made of graphite material or graphite felt. pipe 2
1 is a sheath, a graphite heating element 4 is disposed and supported at a core position, and carbon powder 5 is packed around the outer periphery of the sheath. Note that since the inner diameter of the pipe 21 is larger than the outer diameter of the graphite heating element 4, a clearance 22 is formed. This clearance 22
is open on both sides as shown in the figure, one side is connected to the nitrogen inlet 7 and the other side is connected to the nitrogen outlet 8.
are connected to each other.
発熱体4の両端には、図示したように水冷電極
6が取付けられ、一方の電極から他方の電極へ通
電されることにより、この発熱体4が加熱され
る。 As shown, water-cooled electrodes 6 are attached to both ends of the heating element 4, and the heating element 4 is heated by passing current from one electrode to the other electrode.
運転中における窒素は、窒素流入口7から供給
され、第3図の矢印で示すごとく筒状の発熱体4
の筒内9のみならずクリアランス22にも積極的
に流し、流出口8から排出するようにしてある。 During operation, nitrogen is supplied from the nitrogen inlet 7, and the cylindrical heating element 4 is supplied as shown by the arrow in FIG.
It is configured to actively flow not only into the cylinder 9 but also into the clearance 22 and be discharged from the outlet 8.
上記本発明の装置においては、グラフアイト発
熱体4の外周に溝を切つた場合を示したが、第5
図に概略縦断面図で示すごとく、別個のスペーサ
24でクリアランス22を作ることもできる。 In the above device of the present invention, a case is shown in which a groove is cut on the outer periphery of the graphite heating element 4, but the fifth
The clearance 22 can also be created by a separate spacer 24, as shown in schematic longitudinal section.
あるいはまた、上記本発明の装置において断熱
材兼支持材としての用をなしているカーボンパウ
ダ5の代りに、他の軽量な断熱材、例えばフエル
ト状の適当な材料をその一部または全部に用いれ
ば、最内部の当該パイプ21にかかる断熱材の重
量を軽減できるので、グラフアイト発熱体4の外
周の凸部23、あるいはスペーサ24の個数、配
置を必要最少限にすることもできる。第4図に示
すグラフアイト発熱体の凸部23、あるいは第5
図に示すスペーサ24は、グラフアイト発熱体4
の軸方向の適当な箇所だけにすることもできる。 Alternatively, instead of the carbon powder 5 which serves as both a heat insulating material and a supporting material in the device of the present invention, another lightweight heat insulating material, such as a suitable material in the form of felt, may be used for part or all of it. For example, since the weight of the heat insulating material applied to the innermost pipe 21 can be reduced, the number and arrangement of the protrusions 23 on the outer periphery of the graphite heating element 4 or the spacers 24 can be minimized. The convex portion 23 of the graphite heating element shown in FIG.
The spacer 24 shown in the figure is a graphite heating element 4.
It can also be done only at appropriate locations in the axial direction.
さらにまた、上記本発明の装置においては、ク
リアランス22はグラフアイト発熱体4の外周部
軸方向に設けたが、必ずしも軸方向に限定するも
のでもなく、例えばスペーサ24をリング状にな
し、両端でグラフアイト発熱体4を支持してクリ
アランス部22を形成することも可能である。グ
ラフアイト発熱体4内外周の窒素流方向に就いて
も必ずしも並行である必要はなく、対向させたり
あるいは当該発熱体4の内外周の一方に通気させ
た後、他方へ環流させることもできる。 Furthermore, in the apparatus of the present invention, the clearance 22 is provided in the axial direction of the outer circumference of the graphite heating element 4, but it is not necessarily limited to the axial direction. For example, the spacer 24 may be formed in a ring shape, and It is also possible to form the clearance portion 22 by supporting the graphite heating element 4. The direction of nitrogen flow around the inner and outer peripheries of the graphite heating element 4 does not necessarily have to be parallel; it is also possible to make them face each other, or to let the nitrogen flow through one of the inner and outer peripheries of the graphite heating element 4 and then circulate it to the other.
[実施例]
上述した本発明よる高温加熱装置を用いること
により、以下の実施例に見るような、予想以上の
驚くべき効果を奏することが出来た。[Example] By using the high-temperature heating device according to the present invention described above, surprising effects beyond expectations could be achieved as seen in the following Examples.
比較例 1
第1図に示す従来の黒鉛化炉10において、グ
ラフアイト発熱体4の最高温度部を2500℃、純度
99.999%の窒素を流量8/分に設定して昼夜連
続運転したところ、17日間でグラフアイト発熱体
4は使用に耐え得なくなつた。第2図に使用後の
グラフアイト発熱体4の概略断面図を示すが最高
温度部付近の外周において著しい減耗部4′が見
られ、減耗量は2Kg(全重量の約15%)にも達し
ていた。Comparative Example 1 In the conventional graphitization furnace 10 shown in FIG.
When 99.999% nitrogen was set at a flow rate of 8/min and continuously operated day and night, the graphite heating element 4 became unusable after 17 days. Fig. 2 shows a schematic cross-sectional view of the graphite heating element 4 after use, and a markedly worn part 4' can be seen on the outer periphery near the highest temperature part, and the amount of wasted amount reaches 2 kg (approximately 15% of the total weight). was.
実施例 1
第3図に示した、本発明による黒鉛化炉20を
用い、グラフアイト発熱体4の最高温度部を2500
℃、純度99.999%の窒素の流量を15/分に設定
して昼夜連続運転したところ、驚くべきことにグ
ラフアイト発熱体4の寿命は110日にまで延長さ
れた。Example 1 Using the graphitization furnace 20 according to the present invention shown in FIG.
℃, and the flow rate of 99.999% pure nitrogen was set at 15/min, and the life of the graphite heating element 4 was surprisingly extended to 110 days when it was operated continuously day and night.
以上説明した実施態様においては、黒鉛化繊維
を製造するタンマン炉の場合について説明した
が、高温加熱装置のその目的とするところは必ず
しも限定されるべきものではなく、本発明の主旨
は広く適応できる。また、その加熱手段、装置に
ついても、カーボンあるいはグラフアイトを発熱
体とする高温加熱装置であれば広く応用できる。
あるいはまた、供給する不活性ガスについても窒
素に限定するものではなく、目的に応じて適当に
選択できる。 In the embodiments described above, the case of a Tammann furnace for producing graphitized fibers has been described, but the purpose of the high-temperature heating device is not necessarily limited, and the gist of the present invention can be widely applied. . Moreover, the heating means and apparatus can be widely applied as long as it is a high-temperature heating apparatus using carbon or graphite as a heating element.
Alternatively, the inert gas to be supplied is not limited to nitrogen, and can be appropriately selected depending on the purpose.
[効果]
以上説明したように、本発明の炭素繊維の製造
装置は、前記断熱材と発熱体との間に内径が該発
熱体の外形より大で、かつ、グラフアイトあるい
はカーボンからなるパイプを該パイプが鞘で該発
熱体が芯となる位置に設け、該パイプと発熱体と
の間に形成された間隙部の両側を開口せしめ、該
開口部の片側を前記不活性ガス流入口に、該開口
部の他の片側を前記不活性ガス排出口にそれぞれ
連通せしめた構成としたので、当該発熱体内外表
面の雰囲気温度を適切な範囲で低下させ、したが
つて、当該発熱体の蒸発を抑制するものであるか
ら、従来短命であつた発熱体寿命を著しく延長せ
しめ、当該加熱装置の操業上その目的とする生産
効率の向上、更にはその目的とする生産品目のコ
スト低減に大きく寄与し得るものである。[Effects] As explained above, the carbon fiber manufacturing apparatus of the present invention includes a pipe having an inner diameter larger than the outer diameter of the heating element and made of graphite or carbon between the heat insulating material and the heating element. The pipe is provided at a position where the sheath is the heating element and the heating element is the core, and both sides of the gap formed between the pipe and the heating element are opened, and one side of the opening is connected to the inert gas inlet, Since the other side of the opening is configured to communicate with the inert gas discharge port, the atmospheric temperature on the inner and outer surfaces of the heating element can be lowered within an appropriate range, thereby preventing evaporation of the heating element. This significantly extends the life of the heating element, which was conventionally short-lived, and greatly contributes to improving the production efficiency of the heating equipment, which is the objective, and furthermore, to reducing the cost of the production items that are the objective. It's something you get.
また、前記充填断熱材がカーボンあるいはグラ
フアイトパウダである場合は、クリアランス部を
作る前記パイプがこれを支持する構造にしたた
め、前記パウダの抜き取りをすることなく発熱体
の交換が可能となつた。 Further, when the filling insulation material is carbon or graphite powder, the pipe forming the clearance section supports it, so that the heating element can be replaced without removing the powder.
第1図は、従来用いられていた黒鉛化繊維製造
用タンマン炉の概略横断面図、第2図は第1図に
示すタンマン炉において使用されたグラフアイト
発熱体4の使用後の状況を示す概略横断面図、第
3図は第1図に示すタンマン炉を本発明にしたが
つて改造した実施例を示す概略横断面図、第4図
は、第3図に示したタンマン炉の概略縦断面図、
第5図は、第4図に示したタンマン炉の異なる実
施例を示す概略縦断面図を示す。
1:炭化糸、1′:黒鉛化糸、2:ニツプロー
ラ、3:ニツプローラ、4:グラフアイト発熱
体、4′:グラフアイト発熱体減耗部、5:カー
ボンパウダ、6:水冷電極、7:窒素流入口、
8:窒素流出口、9:グラフアイト発熱体内部、
10:従来の黒鉛化炉、20:改造した黒鉛化
炉、21:パイプ、22…クリアランス部、2
3:グラフアイト発熱体の凸部、24:スペー
サ。
Figure 1 is a schematic cross-sectional view of a conventionally used Tammann furnace for producing graphitized fibers, and Figure 2 shows the state of the graphite heating element 4 used in the Tammann furnace shown in Figure 1 after use. 3 is a schematic cross-sectional view showing an embodiment of the Tammann furnace shown in FIG. 1 modified according to the present invention; FIG. 4 is a schematic vertical cross-sectional view of the Tammann furnace shown in FIG. 3. side view,
FIG. 5 shows a schematic longitudinal sectional view of a different embodiment of the Tammann furnace shown in FIG. 1: Carbonized thread, 1': Graphitized thread, 2: Nippuro roller, 3: Nippuro roller, 4: Graphite heating element, 4': Graphite heating element wear part, 5: Carbon powder, 6: Water-cooled electrode, 7: Nitrogen inlet,
8: Nitrogen outlet, 9: Inside of graphite heating element,
10: Conventional graphitization furnace, 20: Modified graphitization furnace, 21: Pipe, 22...Clearance part, 2
3: Convex portion of graphite heating element, 24: Spacer.
Claims (1)
の発熱体と、該発熱体の両端に設けた電極と、該
発熱体の外周に設けた断熱材と、該発熱体の片側
に設けられ筒内に連通した不活性ガス流入口と、
該発熱体の他の片側に設けられ筒内に連通した不
活性ガス排出口とからなる炭素繊維の製造装置に
おいて、前記断熱材と発熱体との間に内径が該発
熱体の外形より大で、かつ、グラフアイトあるい
はカーボンからなるパイプを、該パイプが鞘で該
発熱体が芯となる位置に設け、該パイプと発熱体
との間に形成された間隙部の両側を開口せしめ、
該開口部の片側を前記不活性ガス流入口に、該開
口部の他の片側を前記不活性ガス排出口にそれぞ
れ連通せしめたことを特徴とする炭素繊維の製造
装置。1. A cylindrical heating element made of graphite or carbon, electrodes provided at both ends of the heating element, a heat insulating material provided around the outer periphery of the heating element, and a cylindrical heating element provided on one side of the heating element and communicating with the inside of the cylinder. an inert gas inlet;
In a carbon fiber manufacturing apparatus comprising an inert gas discharge port provided on the other side of the heating element and communicating with the inside of the cylinder, the space between the heat insulating material and the heating element has an inner diameter larger than the outer diameter of the heating element. , and a pipe made of graphite or carbon is provided at a position where the pipe is a sheath and the heating element is the core, and both sides of the gap formed between the pipe and the heating element are opened,
A carbon fiber manufacturing apparatus characterized in that one side of the opening communicates with the inert gas inlet and the other side of the opening communicates with the inert gas outlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11450979A JPS5643423A (en) | 1979-09-06 | 1979-09-06 | Device for making carbon fiber |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11450979A JPS5643423A (en) | 1979-09-06 | 1979-09-06 | Device for making carbon fiber |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP18512787A Division JPS63152415A (en) | 1987-07-23 | 1987-07-23 | Apparatus for producing carbon fiber |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5643423A JPS5643423A (en) | 1981-04-22 |
| JPS6311448B2 true JPS6311448B2 (en) | 1988-03-14 |
Family
ID=14639532
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11450979A Granted JPS5643423A (en) | 1979-09-06 | 1979-09-06 | Device for making carbon fiber |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5643423A (en) |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5996691A (en) * | 1982-11-24 | 1984-06-04 | 東レ株式会社 | Resistance heating furnace |
| JPS6066740A (en) * | 1983-09-22 | 1985-04-16 | 原 芳秋 | Denture having bed |
| EP0370060A4 (en) * | 1987-06-22 | 1991-09-11 | Jorge M. Parra | Optical instrument |
| JP3018831B2 (en) * | 1993-06-15 | 2000-03-13 | 東レ株式会社 | Heating element |
| JP4733619B2 (en) * | 2006-11-21 | 2011-07-27 | カルソニックカンセイ株式会社 | Vehicle heat storage system |
| JP5787289B2 (en) * | 2011-06-20 | 2015-09-30 | ミクロ電子株式会社 | Heating device using microwaves |
| DE102014003126A1 (en) * | 2014-03-03 | 2015-09-03 | Clariant International Ltd. | Heating device for the production of carbon fibers |
| DE102018108291A1 (en) * | 2018-04-09 | 2019-10-10 | Eisenmann Se | oven |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5831898Y2 (en) * | 1977-08-01 | 1983-07-14 | 東レ株式会社 | Continuous graphitization equipment for carbon fiber |
-
1979
- 1979-09-06 JP JP11450979A patent/JPS5643423A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5643423A (en) | 1981-04-22 |
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