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JP5162351B2 - Sealing equipment for carbonization furnace for carbon fiber production - Google Patents
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JP5162351B2 - Sealing equipment for carbonization furnace for carbon fiber production - Google Patents

Sealing equipment for carbonization furnace for carbon fiber production Download PDF

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JP5162351B2
JP5162351B2 JP2008168571A JP2008168571A JP5162351B2 JP 5162351 B2 JP5162351 B2 JP 5162351B2 JP 2008168571 A JP2008168571 A JP 2008168571A JP 2008168571 A JP2008168571 A JP 2008168571A JP 5162351 B2 JP5162351 B2 JP 5162351B2
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carbonization furnace
fiber bundle
sealing device
furnace
gas
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JP2010007209A (en
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浩成 稲田
伸之 山本
篤志 川村
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Mitsubishi Chemical Corp
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Mitsubishi Chemical Corp
Mitsubishi Rayon Co Ltd
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Description

本発明は、炭素繊維製造用炭化炉(以下、炭化炉と略す。)への外気の流入および炭化炉内のガスの流出を抑制するシール装置に関する。   The present invention relates to a sealing device that suppresses inflow of outside air into a carbon fiber producing carbonization furnace (hereinafter abbreviated as carbonization furnace) and outflow of gas in the carbonization furnace.

炭素繊維は、通常、アクリル繊維等の炭素繊維前駆体束を200〜300℃の酸化性雰囲気の耐炎化炉内で耐炎化処理して耐炎化繊維束を得た後、該耐炎化繊維束をさらに1000℃以上の不活性ガス雰囲気の炭化炉内で炭化処理することにより製造される。
ところで、炭化処理では、炭化炉内に外気が流入して酸化性雰囲気になると、炭素繊維の性能や品質が低下することがある。そのため、炭化炉内の不活性雰囲気を維持するために、通常、炭化炉の繊維束導出入孔に、炭化炉内への外気の流入および炭化炉内のガスの流出を抑制するためのシール装置が取り付けられている。
シール装置としては、例えば、特許文献1には、繊維束の走行方向に沿って膨張室が5段以上10段未満設けられ、炭化炉側から数えて3段目の膨張室より外側の膨張室の少なくとも1つに、繊維束の走行方向に対して直交方向に不活性気体を吐出する気体吐出手段が設置されたラビリンス型のシール装置が開示されている。
特開2001−98428号公報
The carbon fiber is usually obtained by flame-treating a carbon fiber precursor bundle such as acrylic fiber in a flame-resistant furnace in an oxidizing atmosphere of 200 to 300 ° C. to obtain a flame-resistant fiber bundle, and then the flame-resistant fiber bundle is Furthermore, it manufactures by carbonizing in the carbonization furnace of 1000 degreeC or more of inert gas atmosphere.
By the way, in the carbonization treatment, when the outside air flows into the carbonization furnace and becomes an oxidizing atmosphere, the performance and quality of the carbon fiber may be deteriorated. Therefore, in order to maintain an inert atmosphere in the carbonization furnace, a sealing device for suppressing the inflow of outside air into the carbonization furnace and the outflow of gas in the carbonization furnace usually into the fiber bundle lead-in / out hole of the carbonization furnace Is attached.
As the sealing device, for example, in Patent Document 1, five or more stages and less than ten stages of expansion chambers are provided along the traveling direction of the fiber bundle, and the expansion chamber outside the third stage expansion chamber is counted from the carbonization furnace side. In at least one of the above, a labyrinth-type sealing device is disclosed in which gas discharge means for discharging an inert gas in a direction orthogonal to the traveling direction of the fiber bundle is installed.
JP 2001-98428 A

しかしながら、特許文献1に記載のシール装置では、シール性能が必ずしも充分とはいえず、炭化炉内に外気が流入したり、炭化炉内からのガスの流出量が多くなったりすることもあった。特に、炭化炉内の排気ガスを燃焼塔に移送するための排気ガス用配管は、使用時間が長くなるにつれて閉塞するが、排気ガス用配管が閉塞すると、炭化炉内部の圧力が上昇するため、シール装置を介して炭化炉からガスが流出しやすくなった。
本発明は、前記事情に鑑みてなされたものであり、シール性能に優れる上に、炭化炉内の圧力が上昇した場合でも炭化炉からのガスの流出を抑制できる炭素繊維製造用炭化炉のシール装置を提供することを目的とする。
However, in the sealing device described in Patent Document 1, the sealing performance is not always sufficient, and external air may flow into the carbonization furnace or the amount of gas outflow from the carbonization furnace may increase. . In particular, the exhaust gas pipe for transferring the exhaust gas in the carbonization furnace to the combustion tower is closed as the usage time becomes longer, but when the exhaust gas pipe is closed, the pressure inside the carbonization furnace rises, Gas became easier to flow out of the carbonization furnace through the sealing device.
The present invention has been made in view of the above circumstances, and has excellent sealing performance, and even when the pressure in the carbonization furnace is increased, the carbon fiber production carbonization furnace seal capable of suppressing the outflow of gas from the carbonization furnace. An object is to provide an apparatus.

本発明は、以下の構成を有する。
[1] 炭素繊維製造用炭化炉の繊維束導出入孔に接続され、繊維束が通されるラビリンス型のシール装置において、
前記炭化炉の繊維束導出入孔に接続される炭化炉接続孔と外気雰囲気に開放された開放孔とが形成され、内部に繊維束が走行するシール装置本体を有し、
シール装置本体の内部には、繊維束の走行方向に沿って10段以上30段未満の膨張室が設けられ、
開放孔側から数えて8段目の膨張室より炭化炉接続孔側の膨張室の少なくとも1つに、繊維束の走行方向に対して略直交方向に不活性気体を吐出する気体吐出手段が設置されていることを特徴とする炭素繊維製造用炭化炉のシール装置。
[2] 2つの膨張室が互いに対向するように設けられ、該2つの膨張室に気体吐出手段が各々設置されていることを特徴とする[1]に記載の炭素繊維製造用炭化炉のシール装置。
The present invention has the following configuration.
[1] In a labyrinth type sealing device that is connected to a fiber bundle lead-in / out hole of a carbonization furnace for carbon fiber production and through which the fiber bundle is passed,
A carbonization furnace connection hole connected to the fiber bundle lead-in / out hole of the carbonization furnace and an open hole opened to the outside atmosphere are formed, and has a seal device body in which the fiber bundle travels,
Inside the sealing device body, an expansion chamber of 10 stages or more and less than 30 stages is provided along the traveling direction of the fiber bundle,
A gas discharge means for discharging an inert gas in a direction substantially orthogonal to the traveling direction of the fiber bundle is installed in at least one of the expansion chambers on the carbonization furnace connection hole side from the eighth expansion chamber from the open hole side. A carbon furnace sealing device for carbon fiber production, characterized in that
[2] The carbon expansion furnace seal for carbon fiber production according to [1], wherein the two expansion chambers are provided so as to face each other, and gas discharge means are respectively installed in the two expansion chambers. apparatus.

本発明の炭素繊維製造用炭化炉のシール装置は、シール性能に優れる上に、炭化炉内の圧力が上昇した場合でも、シール装置を介した炭化炉からのガスの流出を抑制できる。   The sealing device for a carbon fiber producing carbonization furnace of the present invention is excellent in sealing performance and can suppress the outflow of gas from the carbonizing furnace through the sealing device even when the pressure in the carbonizing furnace rises.

本発明の炭素繊維製造用炭化炉のシール装置(以下、シール装置と略す。)の一実施形態例について説明する。
図1に、本実施形態例のシール装置を示す。このシール装置10は、炭化炉20の繊維束導出入孔21に接続され、繊維束Aが通されるラビリンス型のもので、内部に帯状の繊維束Aが走行するシール装置本体11を有する。
An embodiment of a carbon fiber producing carbonization furnace sealing device (hereinafter abbreviated as a sealing device) according to the present invention will be described.
FIG. 1 shows a sealing device of this embodiment. The sealing device 10 is a labyrinth type device that is connected to the fiber bundle lead-in / out hole 21 of the carbonization furnace 20 and through which the fiber bundle A is passed, and has a seal device body 11 in which the belt-like fiber bundle A travels.

本実施形態例におけるシール装置本体11は、四角柱状の箱体であって、一方の端面11aに、炭化炉20の繊維束導出入孔21に接続される炭化炉接続孔11bが形成され、他方の端面11cに、外気雰囲気30に開放された開放孔11dが形成されている。
本実施形態例における炭化炉接続孔11bおよび開放孔11dは、水平方向が長辺の矩形状の孔である。
The sealing device main body 11 in the present embodiment is a square columnar box, and a carbonization furnace connection hole 11b connected to the fiber bundle lead-in / out hole 21 of the carbonization furnace 20 is formed on one end surface 11a. An open hole 11d that is open to the outside air atmosphere 30 is formed in the end surface 11c.
The carbonization furnace connection hole 11b and the open hole 11d in the present embodiment are rectangular holes having a long side in the horizontal direction.

シール装置本体11の内部には、繊維束Aが走行する方向に沿って15段の膨張室12,12・・・が設けられている。
ここで、膨張室とは、2枚の仕切り板で挟まれた空間のことである。本実施形態例における膨張室12は、シール装置本体11の上面に対して垂直に取り付けられた矩形状の2枚の仕切り板13a,13aで挟まれた空間、および、シール装置本体11の下面に対して垂直に取り付けられた矩形状の2枚の仕切り板13b,13bで挟まれた空間である。すなわち、本実施形態例では、膨張室12は、シール装置本体11の上部および下部に設けられ、上部の膨張室12と下部の膨張室12とが互いに対向するようになっている。
なお、シール装置本体11の炭化炉接続孔11bが形成された一方の端面11aと仕切り板13a,13bとで挟まれた空間14、シール装置本体11の開放孔11dが形成された他方の端面11cと仕切り板13a,13bとで挟まれた空間15は膨張室ではない。実質的に、空間14は炭化炉20の内部と同じ雰囲気になり、空間15は外気と同じ雰囲気になるからである。
Inside the sealing device main body 11, 15 stages of expansion chambers 12, 12... Are provided along the direction in which the fiber bundle A travels.
Here, the expansion chamber is a space sandwiched between two partition plates. The expansion chamber 12 in the present embodiment is formed in a space sandwiched between two rectangular partition plates 13 a and 13 a that are vertically attached to the upper surface of the sealing device body 11, and on the lower surface of the sealing device body 11. It is a space sandwiched between two rectangular partition plates 13b, 13b attached vertically. That is, in the present embodiment, the expansion chambers 12 are provided at the upper and lower portions of the seal device main body 11 so that the upper expansion chamber 12 and the lower expansion chamber 12 face each other.
In addition, the space 14 sandwiched between one end surface 11a in which the carbonizing furnace connection hole 11b of the sealing device body 11 is formed and the partition plates 13a and 13b, and the other end surface 11c in which the opening hole 11d of the sealing device body 11 is formed. And the space 15 sandwiched between the partition plates 13a and 13b is not an expansion chamber. This is because the space 14 has substantially the same atmosphere as the inside of the carbonization furnace 20 and the space 15 has the same atmosphere as the outside air.

本実施形態例では、上側の仕切り板13aと下側の仕切り板13bとが、互いの先端が対向するようにシール装置本体11に取り付けられている。また、本実施形態例では膨張室12の数が15段であるから、仕切り板13a,13bはシール装置本体11の上面または下面に各々16枚取り付けられている。
互いに対向するように仕切り板13a,13bが取り付けられていることにより、水平方向が長辺の矩形状の開口部13cが形成されている。互いに対向する仕切り板13a,13bの間隔は、炭化炉接続孔11bに近くなるほど、大きくなっていることが好ましい。炭化炉20に近くなるにつれて、繊維束Aが自重により撓むため、繊維束Aが下側の仕切り板13bに接触するおそれがあるが、仕切り板13a,13bの間隔が、炭化炉接続孔11bに近くなるほど、大きくなっていれば、繊維束Aの下側の仕切り板13bへの接触を防止しやすい。
In the present embodiment example, the upper partition plate 13a and the lower partition plate 13b are attached to the seal device body 11 so that their tips are opposed to each other. In the present embodiment, the number of expansion chambers 12 is fifteen, so that 16 partition plates 13a and 13b are attached to the upper surface or the lower surface of the seal device main body 11, respectively.
By attaching the partition plates 13a and 13b so as to face each other, a rectangular opening portion 13c having a long side in the horizontal direction is formed. It is preferable that the space | interval of the partition plates 13a and 13b which oppose each other becomes so large that it is close to the carbonization furnace connection hole 11b. As the fiber bundle A bends due to its own weight as it becomes closer to the carbonization furnace 20, the fiber bundle A may come into contact with the lower partition plate 13b. However, the interval between the partition plates 13a and 13b is set to the carbonization furnace connection hole 11b. If it is larger, the contact with the lower partition plate 13b of the fiber bundle A can be easily prevented.

繊維束Aの走行方向に沿って隣接する仕切り板13a,13a、または、仕切り板13b,13bの間隔は、炭化炉20の大きさに応じて適宜選択されるが、例えば、5〜20cmであることが好ましい。仕切り板13a,13aまたは仕切り板13b,13bの間隔が5cm以上であれば、シール性能をより高めることができ、20cm以下であれば、シール装置10全体が大きくなりすぎず、設置場所を容易に確保できる。   Although the space | interval of the partition plates 13a and 13a adjacent to the running direction of the fiber bundle A or the partition plates 13b and 13b is suitably selected according to the magnitude | size of the carbonization furnace 20, it is 5-20 cm, for example. It is preferable. If the interval between the partition plates 13a and 13a or the partition plates 13b and 13b is 5 cm or more, the sealing performance can be further improved. If the interval is 20 cm or less, the entire sealing device 10 does not become too large, and the installation place is easy. It can be secured.

また、仕切り板13a,13bは、シール装置本体11の内部の清掃がしやすくなり、メンテナンス性に優れることから、シール装置本体11に着脱可能に取り付けられていることが好ましい。   Moreover, it is preferable that the partition plates 13a and 13b are detachably attached to the seal device body 11 because the inside of the seal device body 11 can be easily cleaned and is excellent in maintainability.

シール装置本体11および仕切り板13a,13bを構成する材料としては、耐熱性に優れた材料を用いることが好ましく、具体的には、黒鉛が好ましい。シール装置本体11および仕切り板13a,13bを構成する材料として黒鉛を用いれば、熱変形しにくく、寸法安定性に優れるため、繊維束Aの走行位置を正確に制御することでシール装置本体11や仕切り板13a,13bとの接触を防止できる。また、繊維束Aがシール装置本体11や仕切り板13a,13bに接触したとしても、黒鉛は自己潤滑性が良好であるため、繊維束Aの損傷を小さくすることができる。また、寸法安定性に優れるため、仕切り板13a,13bを印籠嵌めによりシール装置本体11に着脱可能に取り付けることができ、ボルト類による固定が不要になり、シール装置本体11からの仕切り板13a,13bの取り外し作業が簡便になる。さらに、黒鉛は軽量であるため、清掃等のメンテナンスを行う際に、シール装置10を炭化炉20から取り外す作業などが容易になる。   As a material constituting the sealing device body 11 and the partition plates 13a and 13b, a material having excellent heat resistance is preferably used, and specifically, graphite is preferable. If graphite is used as the material constituting the sealing device main body 11 and the partition plates 13a and 13b, it is difficult to be thermally deformed and excellent in dimensional stability. Therefore, the traveling position of the fiber bundle A can be accurately controlled to control the sealing device main body 11 and Contact with the partition plates 13a and 13b can be prevented. Further, even if the fiber bundle A comes into contact with the sealing device main body 11 and the partition plates 13a and 13b, the damage of the fiber bundle A can be reduced because graphite has good self-lubricity. In addition, since the dimensional stability is excellent, the partition plates 13a and 13b can be detachably attached to the seal device main body 11 by fitting the seals, and fixing with bolts is not necessary, and the partition plates 13a and 13 The removal work of 13b becomes simple. Further, since graphite is lightweight, it is easy to remove the sealing device 10 from the carbonization furnace 20 when performing maintenance such as cleaning.

図2に示すように、本実施形態例のシール装置10においては、開放孔11d側から数えて15段目の上下の膨張室12a,12b(すなわち、最も炭化炉接続孔11b側の膨張室12a,12b)の各々に、気体吐出手段16が1つずつ設置されている。このように各膨張室12a,12bに気体吐出手段16が1つずつ配置されていると、シール性能がより高くなる。   As shown in FIG. 2, in the sealing device 10 according to the present embodiment, the upper and lower expansion chambers 12a and 12b (that is, the expansion chamber 12a closest to the carbonization furnace connection hole 11b) are counted from the open hole 11d side. , 12b), one gas discharge means 16 is installed. Thus, when the gas discharge means 16 is arrange | positioned 1 each in each expansion chamber 12a, 12b, sealing performance will become higher.

気体吐出手段16とは、繊維束Aの走行方向に対して直交方向に不活性気体(例えば、窒素ガス、アルゴンガス等)を吐出するものである。
本実施形態例における気体吐出手段16は、長さ方向に沿って吐出孔16aが多数形成された金属製の管である。また、本実施形態例における吐出孔16aは、繊維束Aと反対側に向けられて、不活性気体が繊維束Aの走行方向と略直交方向に吐出されるようになっている。
The gas discharge means 16 discharges an inert gas (for example, nitrogen gas, argon gas, etc.) in a direction orthogonal to the traveling direction of the fiber bundle A.
The gas discharge means 16 in the present embodiment is a metal tube in which a large number of discharge holes 16a are formed along the length direction. Further, the discharge hole 16a in the present embodiment is directed to the opposite side of the fiber bundle A, and the inert gas is discharged in a direction substantially orthogonal to the traveling direction of the fiber bundle A.

本実施形態例では、最も炭化炉接続孔11b側の膨張室12に、多数の孔が形成された多孔板17が水平に設けられている。この多孔板17によって、不活性気体が均一に繊維束A方向に吐出するようになっている。
多孔板17の材質としては、熱変形しにくいことから、黒鉛が好ましい。
In this embodiment, a porous plate 17 having a large number of holes is horizontally provided in the expansion chamber 12 closest to the carbonization furnace connection hole 11b. The perforated plate 17 discharges the inert gas uniformly in the direction of the fiber bundle A.
The material of the porous plate 17 is preferably graphite because it is difficult to be thermally deformed.

シール装置10に通される繊維束Aは、アクリロニトリル100%のアクリル繊維またはアクリロニトリルを少なくとも90%以上含有するアクリル系共重合繊維を耐炎化処理した帯状の繊維束、または、炭化炉20にて炭化処理された帯状の繊維束である。
繊維束Aの総繊度は、繊維束Aの強度や処理効率の点から、300テックス以上であることが好ましい。
The fiber bundle A passed through the sealing device 10 is a belt-like fiber bundle obtained by flame-treating 100% acrylonitrile acrylic fiber or acrylic copolymer fiber containing at least 90% acrylonitrile, or carbonized in a carbonization furnace 20. It is the processed strip-shaped fiber bundle.
The total fineness of the fiber bundle A is preferably 300 tex or more from the viewpoint of the strength and processing efficiency of the fiber bundle A.

シール装置10が取り付けられる炭化炉20は、上方および下方にヒータ23が設けられて、耐炎化処理後の繊維束Aが炭化処理される熱処理室22を有している。この熱処理室22の端部が繊維束導出入孔21になっている。したがって、炭化炉20の熱処理室22にシール装置10が接続されている。   The carbonization furnace 20 to which the sealing device 10 is attached has a heat treatment chamber 22 in which heaters 23 are provided above and below, and the fiber bundle A after the flameproofing treatment is carbonized. An end portion of the heat treatment chamber 22 is a fiber bundle outlet / inlet 21. Therefore, the sealing device 10 is connected to the heat treatment chamber 22 of the carbonization furnace 20.

上記シール装置10は、以下のようにして使用される。
すなわち、シール装置10を炭化炉20に、シール装置10の炭化炉接続孔11bが炭化炉20の繊維束導出入孔21に接続されるように取り付ける。
次いで、炭化炉20の熱処理室22をヒータ23により加熱し、シール装置10の開放孔11dから繊維束Aを、繊維束Aの幅方向が水平になるようにシール装置本体11内に導入する。シール装置本体11内に導入された繊維束Aは、シール装置本体11内を走行し、炭化炉接続孔11bおよび繊維束導出入孔21を介して、熱処理室22に導入される。そして、熱処理室22内に導入された繊維束Aは加熱されて炭化処理される。
その際、シール装置10においては、炭化炉接続孔11bに最も近い膨張室12にて気体吐出手段16より不活性気体を繊維束Aの走行方向に対して略直交方向に吐出する。吐出された不活性気体は、シール装置本体11の内壁11eに衝突した後、反転し、仕切り板13a,13bに沿って繊維束Aの方向に流れる。そして、多孔板17を通過した後、隣の膨張室12に流れ込み、さらに隣の膨張室12に流れ込む。このようなことが外側の膨張室12に向かって順次繰り返され、最終的には、各膨張室12に不活性気体が充満すると共に開放孔11dから不活性気体が流出する。これにより、炭化炉20の熱処理室22と外気雰囲気30とを遮断して、シール性能を得る。
また、熱処理室22にて処理された繊維束Aは、炭化炉接続孔11bおよび繊維束導出入孔21を介して、シール装置本体11内に導入される。シール装置本体11内に導入された繊維束Aは、シール装置本体11内を走行し、開放孔11dから外気雰囲気30に導出される。
その際にも、上記のようにシール装置10では、気体吐出手段16から不活性気体を吐出して、各膨張室12に不活性気体を充満させると共に開放孔11dから不活性気体を流出させて、シール性能を得る。
The sealing device 10 is used as follows.
That is, the sealing device 10 is attached to the carbonization furnace 20 so that the carbonization furnace connection hole 11b of the sealing device 10 is connected to the fiber bundle lead-in / out hole 21 of the carbonization furnace 20.
Next, the heat treatment chamber 22 of the carbonization furnace 20 is heated by the heater 23, and the fiber bundle A is introduced into the sealing device body 11 from the open hole 11 d of the sealing device 10 so that the width direction of the fiber bundle A is horizontal. The fiber bundle A introduced into the sealing device body 11 travels through the sealing device body 11 and is introduced into the heat treatment chamber 22 through the carbonization furnace connection hole 11b and the fiber bundle lead-in / out hole 21. The fiber bundle A introduced into the heat treatment chamber 22 is heated and carbonized.
At that time, in the sealing device 10, the inert gas is discharged from the gas discharge means 16 in a direction substantially orthogonal to the traveling direction of the fiber bundle A in the expansion chamber 12 closest to the carbonization furnace connection hole 11 b. The discharged inert gas collides with the inner wall 11e of the sealing device body 11, and then reverses and flows in the direction of the fiber bundle A along the partition plates 13a and 13b. Then, after passing through the perforated plate 17, it flows into the adjacent expansion chamber 12 and further flows into the adjacent expansion chamber 12. Such a process is sequentially repeated toward the outer expansion chamber 12, and finally, each of the expansion chambers 12 is filled with the inert gas and the inert gas flows out from the open hole 11 d. As a result, the heat treatment chamber 22 and the outside air atmosphere 30 of the carbonization furnace 20 are shut off to obtain sealing performance.
Further, the fiber bundle A processed in the heat treatment chamber 22 is introduced into the seal device main body 11 through the carbonization furnace connection hole 11 b and the fiber bundle lead-in / out hole 21. The fiber bundle A introduced into the sealing device main body 11 travels inside the sealing device main body 11, and is led out to the outside air atmosphere 30 from the open hole 11d.
At that time, as described above, the sealing device 10 discharges the inert gas from the gas discharge means 16 to fill each of the expansion chambers 12 with the inert gas, and causes the inert gas to flow out from the open holes 11d. , Get sealing performance.

上記シール装置10の使用方法においては、気体吐出手段16から吐出する不活性気体を加熱しておくことが好ましい。不活性気体を加熱しておけば、不活性気体が炭化炉20内に流入しても、炭化炉20内の温度ムラが起き難い。
また、気体吐出手段16による不活性気体の吐出では、風速を0.01m/秒以上かつ0.3m/秒以下にすることが好ましい。不活性気体の風速を0.01m/秒以上にすれば、シール性能をより高くできる。一方、不活性気体の風速を0.3m/秒以下にすれば、繊維束Aの走行姿勢の乱れを防止でき、繊維束Aが仕切り板13a,13bの縁に触れて損傷することを防止できる。さらには、不活性気体の使用量を抑制でき、製造コストを低くすることができる。
また、炭化炉20の内部の圧力が上昇する場合には、シール性能の低下を抑制するために、圧力上昇に対応して不活性気体の風速を速くすることが好ましい。
In the usage method of the sealing device 10, it is preferable to heat the inert gas discharged from the gas discharge means 16. If the inert gas is heated, even if the inert gas flows into the carbonization furnace 20, temperature unevenness in the carbonization furnace 20 hardly occurs.
Moreover, in the discharge of the inert gas by the gas discharge means 16, it is preferable to make a wind speed into 0.01 m / second or more and 0.3 m / second or less. If the wind speed of the inert gas is 0.01 m / second or more, the sealing performance can be further improved. On the other hand, if the wind speed of the inert gas is set to 0.3 m / second or less, the running posture of the fiber bundle A can be prevented, and the fiber bundle A can be prevented from touching and damaging the edges of the partition plates 13a and 13b. . Furthermore, the amount of inert gas used can be suppressed, and the manufacturing cost can be reduced.
Further, when the pressure inside the carbonization furnace 20 increases, it is preferable to increase the wind speed of the inert gas in response to the pressure increase in order to suppress a decrease in sealing performance.

上記のようなシール装置10では、不活性気体の吐出が、開放孔11d側から数えて8段目の膨張室12より炭化炉接続孔11b側の膨張室12で行われるため、シール装置本体11の内部の各膨張室12に不活性気体を充分に充満させてから、外気に流出させている。そのため、炭化炉20の熱処理室22と外気雰囲気30との間に、不活性気体で充満した空間が充分に存在するようになるため、シール性能が高くなっている。その結果、炭化炉20の内部への外気の流入および炭化炉20からのシール装置10を介したガスの流出を充分に抑制できるようになっている。特に、炭化炉20に接続された排気ガス用配管が閉塞して炭化炉20内部の圧力が上昇した場合でも、シール装置10を介した炭化炉20からのガスの流出を抑制できる。   In the sealing device 10 as described above, the discharge of the inert gas is performed in the expansion chamber 12 on the carbonization furnace connection hole 11b side from the expansion chamber 12 on the eighth stage counted from the open hole 11d side. After each of the expansion chambers 12 is sufficiently filled with an inert gas, it is discharged to the outside air. Therefore, since the space filled with the inert gas is sufficiently present between the heat treatment chamber 22 of the carbonization furnace 20 and the outside air atmosphere 30, the sealing performance is high. As a result, the inflow of outside air into the carbonization furnace 20 and the outflow of gas from the carbonization furnace 20 through the sealing device 10 can be sufficiently suppressed. In particular, even when the exhaust gas pipe connected to the carbonization furnace 20 is closed and the pressure inside the carbonization furnace 20 is increased, the outflow of gas from the carbonization furnace 20 through the seal device 10 can be suppressed.

なお、本発明のシール装置は、上記実施形態例に限定されない。例えば、上記の実施形態例において、互いに対向する上下の膨張室12,12のいずれか一方のみに気体吐出手段16が設けられていても構わない。また、気体吐出手段16が設置された膨張室12に多孔板17が設けられていなくて構わない。
また、シール装置本体11の内部の膨張室12の数は、10段以上30段未満の範囲であればよい。膨張室12の数が10段未満であると、充分なシール性能が得られず、30段以上であると、シール装置10が大きくなるため、設置場所の確保が難しくなる。
また、上記実施形態例では、気体吐出手段16が炭化炉接続孔11bに最も近い膨張室12のみに設置されていたが、本発明では、開放孔11d側から数えて8段目の膨張室12より炭化炉接続孔11b側の膨張室12の少なくとも1つに設置されていればよい。開放孔11d側から数えて8段目の膨張室12より炭化炉接続孔11b側の膨張室12の少なくとも1つに気体吐出手段16が設置されていれば、シール装置10のシール性能を高くすることができる。しかし、圧力変化の傾斜が大きくなってシール性能をより高くできることから、上記実施形態例のように、気体吐出手段16が炭化炉接続孔11bに最も近い膨張室12のみに設置されていることが好ましい。
また、仕切り板13a,13bは、先端が互いに対向していなくてもよい。その場合、膨張室12の段数は、上側の膨張室12と下側の膨張室12とで別々に数える。
また、シール装置本体11は、四角形状の箱体でなくてもよく、例えば、円柱状の箱体であってもよいし、他の多角形状(例えば、三角形状、五角形状等)の箱体であってもよい。
The sealing device of the present invention is not limited to the above embodiment. For example, in the above embodiment, the gas discharge means 16 may be provided only in one of the upper and lower expansion chambers 12 and 12 facing each other. Further, the porous plate 17 may not be provided in the expansion chamber 12 in which the gas discharge means 16 is installed.
Further, the number of expansion chambers 12 inside the sealing device main body 11 may be in a range of 10 steps or more and less than 30 steps. If the number of expansion chambers 12 is less than 10 stages, sufficient sealing performance cannot be obtained. If the number of expansion chambers 12 is 30 stages or more, the sealing device 10 becomes large, and it is difficult to secure an installation location.
In the above embodiment, the gas discharge means 16 is installed only in the expansion chamber 12 closest to the carbonization furnace connection hole 11b. However, in the present invention, the expansion chamber 12 in the eighth stage counted from the open hole 11d side. It should just be installed in at least one of the expansion chambers 12 on the carbonization furnace connection hole 11b side. If the gas discharge means 16 is installed in at least one of the expansion chambers 12 on the carbonization furnace connection hole 11b side from the expansion chamber 12 on the eighth stage counted from the open hole 11d side, the sealing performance of the sealing device 10 is enhanced. be able to. However, since the inclination of the pressure change is increased and the sealing performance can be further improved, the gas discharge means 16 may be installed only in the expansion chamber 12 closest to the carbonization furnace connection hole 11b as in the above embodiment. preferable.
Further, the ends of the partition plates 13a and 13b may not face each other. In that case, the number of stages of the expansion chamber 12 is counted separately for the upper expansion chamber 12 and the lower expansion chamber 12.
Further, the sealing device main body 11 may not be a rectangular box, but may be, for example, a cylindrical box, or another polygonal (for example, triangular, pentagonal, etc.) box. It may be.

(実施例及び比較例)
以下、本発明について具体的な実施例及び比較例を挙げて説明する。
この実施例及び比較例においては、繊維束として総繊度が1000テックスのアクリロニトリル100%のアクリル繊維を耐炎化した繊維束を採用している。
炭化炉としては横型炭化炉を用い、その繊維束導入孔及び導出孔には、黒鉛材の図1および図2に示すシール装置を取り付けた。
であって、その膨張室数等をそれぞれ以下の表1に示す条件としたシール装置を使用して、以下に示す条件を同一として炭化を行った。
炭化炉への投入繊維束数 : 200
炭化炉での処理時間 : 1.5分
炭化炉内温度 : 1000℃
炭化炉及びシール装置の開口幅: 1.3m
シール装置の繊維束走行間隙D: 13mm
炭化炉の開口高さ : 80mm
(Examples and Comparative Examples)
Hereinafter, the present invention will be described with specific examples and comparative examples.
In this example and comparative example, a fiber bundle obtained by making flame resistance of 100% acrylonitrile acrylic fiber having a total fineness of 1000 tex is used as the fiber bundle.
A horizontal carbonization furnace was used as the carbonization furnace, and the sealing device shown in FIGS. 1 and 2 for the graphite material was attached to the fiber bundle introduction hole and the lead-out hole.
Then, carbonization was performed under the same conditions shown below by using a sealing device in which the number of expansion chambers and the like were the conditions shown in Table 1 below.
Number of fiber bundles input into the carbonization furnace: 200
Treatment time in the carbonization furnace: 1.5 minutes Temperature in the carbonization furnace: 1000 ° C
Opening width of carbonization furnace and sealing device: 1.3m
Fiber bundle travel gap D of the sealing device: 13 mm
Opening height of carbonization furnace: 80mm

Figure 0005162351
Figure 0005162351

実施例1では、膨張室を15段とし、開放孔側から数えて15段目に不活性気体の気体吐出手段を設置して、不活性気体を吐出面風速0.07m/秒で吐出した。炭化炉内の圧力は5Paであった。その結果、炉内への外気の流入及び炭化炉からシール装置を介した炉内ガスの流出も無く、シール性能が良好であった。
実施例2は、膨張室、気体吐出手段の設置段数、不活性気体の吐出面風速は実施例1と同一であるが、炭化炉内の圧力は8Paであった。その結果、炉内への外気の流入及び炭化炉からシール装置を介した炉内ガスの流出も無く、シール性能が良好であった。
これに対し、比較例1では、膨張室数、不活性気体の吐出面風速、炭化炉内の圧力は実施例1と同一であるが、開放孔側から数えて3段目に不活性気体の気体吐出手段を設置したシール装置を用いた。その結果、炉内への外気の流入は無いが、炭化炉からシール装置を介した炉内ガスの流出があり、シール性能が不十分であった。
比較例2は、不活性気体の吐出面風速、炭化炉内の圧力は実施例1と同一であるが、膨張室を7段とし、開放孔側から数えて3段目に不活性気体の気体吐出手段を設置した。その結果、炉内への外気の流入は無いが、炭化炉からシール装置を介した炉内ガスの流出があり、シール性能が不充分であった。
In Example 1, the expansion chamber has 15 stages, and an inert gas gas discharge means is installed on the 15th stage from the open hole side, and the inert gas is discharged at a discharge surface wind speed of 0.07 m / sec. The pressure in the carbonization furnace was 5 Pa. As a result, there was no inflow of outside air into the furnace and outflow of furnace gas from the carbonization furnace through the sealing device, and the sealing performance was good.
In Example 2, the expansion chamber, the number of installation stages of the gas discharge means, and the discharge surface wind speed of the inert gas were the same as in Example 1, but the pressure in the carbonization furnace was 8 Pa. As a result, there was no inflow of outside air into the furnace and outflow of furnace gas from the carbonization furnace through the sealing device, and the sealing performance was good.
On the other hand, in Comparative Example 1, the number of expansion chambers, the discharge surface wind speed of the inert gas, and the pressure in the carbonization furnace are the same as those in Example 1, but the inert gas in the third stage counted from the open hole side. A sealing device provided with gas discharge means was used. As a result, there was no inflow of outside air into the furnace, but there was outflow of in-furnace gas from the carbonization furnace through the sealing device, and the sealing performance was insufficient.
In Comparative Example 2, the discharge surface wind speed of the inert gas and the pressure in the carbonization furnace are the same as in Example 1, but the expansion chamber has seven stages and the inert gas gas in the third stage counting from the open hole side. Discharge means was installed. As a result, there was no inflow of outside air into the furnace, but there was outflow of in-furnace gas from the carbonization furnace through the sealing device, and the sealing performance was insufficient.

本発明のシール装置の一実施形態例を示す断面図である。It is sectional drawing which shows one Embodiment of the sealing apparatus of this invention. 図1に示すシール装置における炭化炉接続孔に最も近い膨張室を示す拡大断面図である。It is an expanded sectional view which shows the expansion chamber nearest to the carbonization furnace connection hole in the sealing device shown in FIG.

符号の説明Explanation of symbols

10 シール装置
11 シール装置本体
11a 一方の端面
11b 炭化炉接続孔
11c 他方の端面
11d 開放孔
12,12a,12b 膨張室
13a,13b 仕切り板
13c 開口部
16 気体吐出手段
16a 吐出孔
17 多孔板
20 炭化炉
21 繊維束導出入孔
22 熱処理室
23 ヒータ
30 外気雰囲気
A 繊維束
DESCRIPTION OF SYMBOLS 10 Sealing device 11 Sealing device main body 11a One end surface 11b Carbonization furnace connection hole 11c The other end surface 11d Open hole 12, 12a, 12b Expansion chamber 13a, 13b Partition plate 13c Opening part 16 Gas discharge means 16a Discharge hole 17 Perforated plate 20 Carbonization Furnace 21 Fiber bundle lead-out hole 22 Heat treatment chamber 23 Heater 30 Outside air atmosphere A Fiber bundle

Claims (2)

炭素繊維製造用炭化炉の繊維束導出入孔に接続され、繊維束が通されるラビリンス型のシール装置において、
前記炭化炉の繊維束導出入孔に接続される炭化炉接続孔と外気雰囲気に開放された開放孔とが形成され、内部に繊維束が走行するシール装置本体を有し、
シール装置本体の内部には、繊維束の走行方向に沿って10段以上30段未満の膨張室が設けられ、
開放孔側から数えて8段目の膨張室より炭化炉接続孔側の膨張室の少なくとも1つに、繊維束の走行方向に対して略直交方向に不活性気体を吐出する気体吐出手段が設置されていることを特徴とする炭素繊維製造用炭化炉のシール装置。
In a labyrinth type sealing device that is connected to a fiber bundle lead-in / out hole of a carbonization furnace for carbon fiber production and through which the fiber bundle is passed,
A carbonization furnace connection hole connected to the fiber bundle lead-in / out hole of the carbonization furnace and an open hole opened to the outside atmosphere are formed, and has a seal device body in which the fiber bundle travels,
Inside the sealing device body, an expansion chamber of 10 stages or more and less than 30 stages is provided along the traveling direction of the fiber bundle,
A gas discharge means for discharging an inert gas in a direction substantially orthogonal to the traveling direction of the fiber bundle is installed in at least one of the expansion chambers on the carbonization furnace connection hole side from the eighth expansion chamber from the open hole side. A carbon furnace sealing device for carbon fiber production, characterized in that
2つの膨張室が互いに対向するように設けられ、該2つの膨張室に気体吐出手段が各々設置されていることを特徴とする請求項1に記載の炭素繊維製造用炭化炉のシール装置。   The carbon expansion furnace sealing apparatus according to claim 1, wherein two expansion chambers are provided so as to face each other, and gas discharge means are respectively installed in the two expansion chambers.
JP2008168571A 2008-06-27 2008-06-27 Sealing equipment for carbonization furnace for carbon fiber production Expired - Fee Related JP5162351B2 (en)

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