JPH07252726A - Method for graphitization of low-density carbon fiber molded form - Google Patents

Method for graphitization of low-density carbon fiber molded form

Info

Publication number
JPH07252726A
JPH07252726A JP3343662A JP34366291A JPH07252726A JP H07252726 A JPH07252726 A JP H07252726A JP 3343662 A JP3343662 A JP 3343662A JP 34366291 A JP34366291 A JP 34366291A JP H07252726 A JPH07252726 A JP H07252726A
Authority
JP
Japan
Prior art keywords
graphite
furnace
carbon fiber
case
fiber molded
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.)
Granted
Application number
JP3343662A
Other languages
Japanese (ja)
Other versions
JP3042554B2 (en
Inventor
Isao Nakano
勲 中野
Akio Kato
明男 加藤
Akira Yasojima
亮 八十島
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.)
Tokai Carbon Co Ltd
Mitsubishi Chemical Corp
Original Assignee
Tokai Carbon Co Ltd
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 Tokai Carbon Co Ltd, Mitsubishi Chemical Corp filed Critical Tokai Carbon Co Ltd
Priority to JP3343662A priority Critical patent/JP3042554B2/en
Publication of JPH07252726A publication Critical patent/JPH07252726A/en
Application granted granted Critical
Publication of JP3042554B2 publication Critical patent/JP3042554B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Inorganic Fibers (AREA)

Abstract

PURPOSE:To provide a method for graphitization of low-density carbon fiber molded form, designed to obtain a product less apt to deform and excellent in producibility and quality, etc. CONSTITUTION:Carbon fiber molded forms each <=1.0g/cm<3> in density are put into graphite vessels 1 which are, in turn, embedded in packing coke 2 and then subjected to graphitization treatment.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は低密度炭素繊維成型体の
黒鉛化処理方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for graphitizing a low density carbon fiber molded body.

【0002】[0002]

【従来の技術】低密度炭素繊維成型体は、炭素繊維断熱
材や炭素繊維−炭素複合材料(C/C複合材料)の前駆
体として用いられ、これを黒鉛化処理してC/C複合材
料を得ている。この黒鉛化処理においては、通常抵抗加
熱式炉、誘導加熱式炉等が用いられている。
2. Description of the Related Art A low-density carbon fiber molding is used as a precursor of a carbon fiber heat insulating material or a carbon fiber-carbon composite material (C / C composite material), and is graphitized to obtain a C / C composite material. Is getting In this graphitization treatment, a resistance heating type furnace, an induction heating type furnace, etc. are usually used.

【0003】[0003]

【発明が解決しようとする課題】しかしながら従来の黒
鉛化処理においては、炉詰め効率が悪く、特に円筒状の
形状を持つ製品を処理する場合等は、特に効率が低く、
大量に処理することができなかった。そして効率の悪さ
は直接コストに影響し、大きな課題となっていた。又、
このような課題を解決すべく、電極材、人造黒鉛材等を
黒鉛化処理するので多く用いられるアチソン炉を用いよ
うとしても、電気抵抗が高いため、うまく通電し、自己
発熱させることができず、異常発熱等を生じてしまい、
製品に処理温度むらが生じやすいこと、炉圧(パッキン
グコークス重量による)のため製品にクリープ割れや変
形を生じやすいこと、炉中への洩れ込み空気により、処
理する品物が酸化消耗しやすいこと、パッキングコーク
ス中等に含まれる不純物によって製品の汚染料が大きく
なりやすい、等の課題があり、実現困難であった。
However, in the conventional graphitization treatment, the efficiency of filling in the furnace is low, and particularly when treating a product having a cylindrical shape, the efficiency is low,
It was not possible to process a large amount. And the inefficiency directly affects the cost, which is a big problem. or,
In order to solve such a problem, even if an attempt is made to use an Acheson furnace that is often used for graphitizing electrode materials, artificial graphite materials, etc., because of high electric resistance, it is difficult to energize and self-heat. , Causing abnormal heat generation,
The product is likely to have uneven processing temperature, the product is prone to creep cracking or deformation due to the furnace pressure (due to the packing coke weight), and the air to be leaked into the product tends to oxidize and exhaust the product to be processed. It was difficult to realize such problems as impurities in the packing coke, etc., tended to increase the amount of contaminants in the product.

【0004】[0004]

【課題を解決するための手段】そこで本発明者らは、鋭
意検討の結果、単にアチソン炉中で黒鉛化処理するので
はなく、適当な炭素繊維成型体を、黒鉛材製の容器に収
めたうえ、パッキングコークス中に埋め込んで黒鉛化処
理するならば、かかる課題を解決しうることを見出し、
本発明に到達した。すなわち本発明の目的は、良質の炭
素繊維断熱材やC/C複合材料を安価かつ大量に製造し
うる方法を提供することにあり、かかる目的は、密度
1.0g/cm3以下の炭素繊維成型体を黒鉛材製の容
器に収め、パッキングコークス中に埋め込んで、その後
黒鉛化処理することを特徴とする低密度炭素繊維成型体
の黒鉛化処理方法、により容易に達成される。以下本発
明をより詳細に説明する。
Therefore, as a result of earnest studies, the inventors of the present invention put an appropriate carbon fiber molded body in a container made of a graphite material instead of simply performing the graphitization treatment in an Acheson furnace. Moreover, it was found that such a problem could be solved by embedding in packing coke and performing graphitization treatment,
The present invention has been reached. That is, an object of the present invention is to provide a method capable of inexpensively mass-producing a high-quality carbon fiber heat insulating material and a C / C composite material, and an object of the present invention is to provide a carbon fiber having a density of 1.0 g / cm 3 or less. This is easily achieved by a method for graphitizing a low-density carbon fiber molded body, which is characterized in that the molded body is placed in a container made of a graphite material, embedded in packing coke, and then graphitized. The present invention will be described in more detail below.

【0005】本発明に使用する、炭素繊維成型体は、主
として炭素繊維から成り、一般にC/C複合材等の原材
料として用いられるものであれば特に限定せれず、その
密度は1.0g/cm3以下、より好ましくは0.5g
/cm3以下である。密度が1.0g/cm3を越える
と、変形等の問題を生じる公算が小さくなるので、本発
明の方法を用いる価値が小さい。本発明の黒鉛化処理に
おいては、熱処理すべき低密度炭素繊維成型体は黒鉛ケ
ース内に収めて処理される。黒鉛ケース(図1)の大き
さ(外寸)は後述の諸要因によって決められるが通常L
は〜2.5m、Wは0.2〜1m、好ましくは0.2〜
0.5mの範囲、Hは〜1.8mの大きさである。黒鉛
ケースは必ずしも一体物である必要はなく、適当な大き
さの黒鉛板を適宣組み合せて作っても良い。ただし、こ
の場合黒鉛ケースとして形を保てる様にするため、さら
には内部に収める成型体の酸化消耗を出来るだけ低減す
るため密封性を高めることが望ましく、図2に示す様な
ホゾ方式、インロー方式、落し蓋方式等により組立てる
ことが好ましい。
The carbon fiber molded body used in the present invention is mainly composed of carbon fibers and is not particularly limited as long as it is generally used as a raw material such as a C / C composite material, and its density is 1.0 g / cm. 3 or less, more preferably 0.5 g
/ Cm 3 or less. If the density exceeds 1.0 g / cm 3 , the possibility of causing problems such as deformation becomes small, and thus the value of using the method of the present invention is small. In the graphitization treatment of the present invention, the low-density carbon fiber molded body to be heat-treated is placed in a graphite case for treatment. The size (outer size) of the graphite case (Fig. 1) is usually determined by L
Is ~ 2.5 m, W is 0.2-1 m, preferably 0.2-
In the range of 0.5 m, H has a size of ˜1.8 m. The graphite case does not necessarily have to be an integral body, and may be made by appropriately combining graphite plates having an appropriate size. However, in this case, it is desirable to enhance the sealing property in order to keep the shape of the graphite case and further to reduce the oxidation consumption of the molded body housed inside. It is preferable to assemble by a drop lid method or the like.

【0006】黒鉛ケースあるいは黒鉛ケースを組み立て
るための黒鉛板の厚さは取扱い重量、負荷重量と発熱の
させやすさとの兼ね合いになる。厚さが大であると黒鉛
ケース自体の重量も大となり炉への出し入れが困難とな
るし、またケース内に収められる成型体の量も少なくな
ってしまう。一方、厚さが小であるとケース内に収めら
れる成型体の重量あるいはパッキングコースの重量によ
ってケースが破壊する可能性が生じる。したがって10
〜100mm、好ましくは20〜50mmの範囲の厚さ
とすることが望ましい。黒鉛ケースに用いる黒鉛材の電
気比抵抗は3000μΩ・cm以下、好ましくは150
0μΩ・cm以下であることが発熱のさせやすさからみ
て望ましい。
The thickness of the graphite case or the graphite plate for assembling the graphite case is a balance between the handling weight, the load weight and the easiness of heat generation. When the thickness is large, the weight of the graphite case itself becomes large, which makes it difficult to put the graphite case in and out of the furnace, and the amount of the molded body accommodated in the case becomes small. On the other hand, if the thickness is small, the case may be broken due to the weight of the molded body contained in the case or the weight of the packing course. Therefore 10
It is desirable that the thickness is in the range of -100 mm, preferably 20-50 mm. The electrical resistivity of the graphite material used for the graphite case is 3000 μΩ · cm or less, preferably 150
It is desirable that it is 0 μΩ · cm or less from the viewpoint of heat generation.

【0007】黒鉛ケースには収めた成型体の酸化消耗低
減および熱処理後の不純物量低減のため、窒素あるいは
アルゴン等の不活性ガスを導入しても良く、この場合は
黒鉛ケースから炉外パッキングコークス上に導いた黒鉛
パイプを通じてガスを送り込む方法が好ましい。本発明
において用いるアチソン炉の構造の一例を本発明実施態
応として示す。説明図として、炉上から見た状態を図3
に、通電方向に直交する断面で切った状態を図4に示
す。アチソン炉の大きさは一般的には長さ10〜25
m、巾1.2〜2.5m,深さ1.2〜2m程度である
が、この中に成型体を収めた黒鉛ケース1を配置する。
An inert gas such as nitrogen or argon may be introduced into the graphite case in order to reduce oxidation consumption of the molded body contained therein and the amount of impurities after the heat treatment. In this case, the packing coke outside the furnace is introduced from the graphite case. A method of feeding gas through the graphite pipe guided above is preferable. An example of the structure of the Acheson furnace used in the present invention is shown as an embodiment of the present invention. As an explanatory diagram, the state seen from above the furnace is shown in FIG.
FIG. 4 shows a state cut along a cross section orthogonal to the energization direction. The size of the Acheson furnace is generally 10 to 25 in length.
m, the width is 1.2 to 2.5 m, and the depth is 1.2 to 2 m, and the graphite case 1 containing the molded body is arranged therein.

【0008】炉長さ方向には各黒鉛ケースに間隔をとっ
て配置することが必要である。この間隙によって通電ギ
ャップを作り通電抵抗を調節して炉の通電効率すなわち
発熱効率を確保する。間隙は通常10〜100cmの範
囲で調節され、少なくとも5箇所以上設けられることが
望ましいが、その数が多くなると必然的に黒鉛ケースの
大きさが小さくなり、その中に収める低密度炭素繊維成
型体の大きさに制約が生じる。炉の形状が長矩形である
ので、通常は黒鉛ケースの長手方向、Lを炉長方向に揃
えて配置するが上記の事情により黒鉛ケースのLには制
限が生じる。炉巾方向にも各黒鉛ケースに間隔をとって
配置することが望ましい。
It is necessary to arrange the graphite cases at intervals in the furnace length direction. An energization gap is created by this gap and the energization resistance is adjusted to ensure the energization efficiency of the furnace, that is, the heat generation efficiency. The gap is usually adjusted within the range of 10 to 100 cm, and it is desirable to provide at least 5 or more locations. However, if the number is increased, the size of the graphite case is inevitably reduced, and a low density carbon fiber molded body to be housed in the graphite case. There is a restriction on the size of. Since the shape of the furnace is an oblong rectangle, the length L of the graphite case is usually aligned with the lengthwise direction of the furnace. However, due to the above circumstances, the L of the graphite case is limited. It is desirable to arrange the graphite cases in the furnace width direction at intervals.

【0009】すなわち炉内にある黒鉛ケースの主たる発
熱面は通電方向に平行な面となるが、炉の巾方向に複数
の黒鉛ケースを配置して発熱面を分散させることが炉内
の均温性を高めるために望ましい。この場合隣接する黒
鉛ケース同士が接近しすぎていると発熱面が接近するこ
とになり、その部分の温度が相対的に高くなるので5〜
30cmの間隔をとることが望ましい。一般的な炉巾、
複数個の黒鉛ケースを配置すること、およびそれぞれ間
隔をとる必要のあること、より黒鉛ケースのWには制限
が生じる。炉の深さ方向については長さ方向、巾方向の
様な条件はなく、炉深さ一杯の高さ、Hを持つ黒鉛ケー
スを置いても良いし、またHの小さなケースをいくつか
間隔をとらずに積み重ねても良い。ただし、全体の高さ
がパッキングコークス2中に完全に、少なくとも30c
m以上の厚さでもって埋まる範囲であることが酸化消耗
から黒鉛ケースおよび内部の成型体を保護するために必
要である。なお図中、3は炉壁、4は通電端子、5は炉
床を示す。
That is, the main heating surface of the graphite case in the furnace is a surface parallel to the energization direction, but it is possible to disperse the heating surface by disposing a plurality of graphite cases in the width direction of the furnace. Desirable to enhance sex. In this case, if the adjacent graphite cases are too close to each other, the heat generating surfaces will be close to each other, and the temperature of that portion becomes relatively high.
A spacing of 30 cm is desirable. General furnace width,
Due to the arrangement of a plurality of graphite cases and the need to provide an interval between them, W of the graphite case is limited. There are no conditions such as length direction and width direction for the depth direction of the furnace. A graphite case with a height of H, H, which is full of the furnace depth, may be placed. You can stack them without taking them. However, the total height is completely at least 30c in the packing coke 2.
It is necessary to have a thickness of at least m in order to protect the graphite case and the internal molded body from oxidation consumption. In the figure, 3 is a furnace wall, 4 is a current-carrying terminal, and 5 is a hearth.

【0010】黒鉛ケースを配置する場合に、通電経路調
節、発熱面調節のために黒鉛ケース以外の黒鉛部材
(板、丸棒等)を適宣配置しても良い。例えば炉の上
面、側面は放熱があるため炉中心部に比べて温度が低く
なり易い。これを防ぐため配置した黒鉛ケースの上面、
炉壁側側面に黒鉛板等を配置することが有効である。前
述の方法によって低密度炭素繊維成型体を黒鉛化処理す
ることが出来るが処理温度をより正確に調節するために
は炉内の温度を測定することが望ましい。この方法とし
ては炉内の黒鉛ケース外表面から炉外パッキングコーク
ス上に導いた、不活性ガスでシールされた黒鉛パイプ6
を通して、黒鉛ケースの外表面を放射温度計で側温する
方法が一般的である。
When arranging the graphite case, a graphite member (a plate, a round bar, etc.) other than the graphite case may be properly arranged for adjusting the electric current path and the heating surface. For example, since the upper surface and side surfaces of the furnace radiate heat, the temperature tends to be lower than that in the central part of the furnace. To prevent this, the top surface of the graphite case,
It is effective to arrange a graphite plate or the like on the side surface on the furnace wall side. The low-density carbon fiber molded body can be graphitized by the above-mentioned method, but it is desirable to measure the temperature in the furnace in order to adjust the processing temperature more accurately. As this method, an inert gas-sealed graphite pipe 6 is introduced from the outer surface of the graphite case in the furnace onto the packing coke outside the furnace.
A general method is to laterally heat the outer surface of the graphite case with a radiation thermometer.

【0011】通常黒鉛ケースの通電方向に平行な面の発
熱が早く、垂直な面の発熱は平行な面に比べるて遅れる
ので、この2点の温度を測定し、平行な面の温度が目的
の処理温度に近づいた所で通電量を調節して処理温度を
保持する様にする。そしてこの間に垂直な面の温度が処
理温度に追いついた所で通電を停止すれば全体を均一な
温度で処理することが出来る。以下本発明を実施例を用
いて説明するが、本発明はその要旨を越えない限り実施
例に限定されない。
Generally, the heat generated on the plane parallel to the energization direction of the graphite case is early and the heat generated on the vertical plane is delayed as compared with the parallel plane. Therefore, the temperatures at these two points are measured, and the temperature of the parallel plane is the target. When the temperature approaches the processing temperature, the energization amount is adjusted to maintain the processing temperature. Then, during this time, if the temperature of the vertical surface catches up with the processing temperature and the energization is stopped, the entire surface can be processed at a uniform temperature. Hereinafter, the present invention will be described using examples, but the present invention is not limited to the examples as long as the gist thereof is not exceeded.

【0012】[0012]

【実施例】【Example】

(実施例1)解繊した炭素繊維(三菱化成ダイアリード
K−521)にフェノール樹脂(群栄化学PL−221
1)を含浸した後、熱板プレスして得た成型体をレトル
トタイプの外熱式焼成炉で1000℃まで焼成し、15
00×1000mm、厚さ52mm,平均密度0.19
5g/cm2の低密度炭素繊維成型体を得た。この低密
度炭素繊維成型体を内寸315W×1650L×1190
Hmmの40mm厚さの黒鉛板(電気比抵抗740μΩ
cm)を組合せた黒鉛ケース内に6枚納めたものを14
ケース準備した。この黒鉛ケースを図5の様に炉長15
800mm、炉巾1200mm、炉深1300mmのア
チソン炉中に炉長方向に7列、炉巾方向に2列の配置で
並べた。黒鉛ケース間隔は通電方向で430mm、通電
方向に垂直な方向で80mmとした。
(Example 1) Phenolic resin (Gunei Kagaku PL-221) was added to defibrated carbon fiber (Mitsubishi Kasei Dilead K-521).
After impregnation with 1), the molded body obtained by hot plate pressing is fired to 1000 ° C. in a retort type external heating type firing furnace,
00 × 1000mm, thickness 52mm, average density 0.19
A low-density carbon fiber molded body of 5 g / cm 2 was obtained. This low-density carbon fiber molded body has an inner size of 315 W x 1650 L x 1190
H mm 40 mm thick graphite plate (electrical resistivity 740 μΩ
cm)) 6 pieces in a graphite case
I prepared the case. This graphite case is used as shown in Fig.
In an Acheson furnace of 800 mm, furnace width 1200 mm, furnace depth 1300 mm, 7 rows were arranged in the furnace length direction and 2 rows were arranged in the furnace width direction. The graphite case spacing was 430 mm in the energizing direction and 80 mm in the direction perpendicular to the energizing direction.

【0013】黒鉛ケースを設置した後パッキングコーク
スを充填し、黒鉛ケースの上面より550mmの高さま
で覆った。各黒鉛ケースには内径20mmの黒鉛パイプ
を取付け、パッキングコース外からN2ガスを流し込め
る様にした。また、炉中心部に設置した黒鉛ケースの通
電方向に平行な端面および垂直な端面より、N2ガスシ
ールした黒鉛パイプを導き、放射温度計で黒鉛ケースの
外表面温度を測定出来る様にした。以上のセットの終っ
た後、まず2l/minの割合で2Hr、黒鉛ケース内
にN2を通気し、その後N2を止めて炉の通電を開始し
た。通電開始後59Hr後に黒鉛ケースの通電方向に平
行な面の温度が2500℃に達したので、投入電力を減
じ、さらに21Hr後に垂直な面の温度が2460℃に
達した所で通電を停止した。通電停止の3Hr前から、
0.5l/minの割合で再び黒鉛ケース内にN2を通
気し、以後冷却を続けて8日後に製品を取り出すまで流
し続けた。炉の冷却が終了した後、パッキングコークス
を取除き、黒鉛ケースを取出して内部の炭素繊維成型体
を取出した。
After the graphite case was installed, packing coke was filled and the graphite case was covered to a height of 550 mm from the upper surface. A graphite pipe having an inner diameter of 20 mm was attached to each graphite case so that N 2 gas could be poured from outside the packing course. In addition, a graphite pipe sealed with N 2 gas was introduced from the end faces parallel to and perpendicular to the energization direction of the graphite case installed in the center of the furnace, and the outer surface temperature of the graphite case could be measured with a radiation thermometer. After completion of the above-mentioned set, first, 2 Hr was aerated at a rate of 2 l / min, N 2 was aerated in the graphite case, and then N 2 was stopped to start the energization of the furnace. The temperature of the plane parallel to the energization direction of the graphite case reached 2500 ° C. 59 hours after the start of energization, so the applied power was reduced, and after 21 hours, the energization was stopped when the temperature of the vertical plane reached 2460 ° C. From 3 hours before the stop of energization,
N 2 was again bubbled into the graphite case at a rate of 0.5 l / min, and cooling was continued thereafter, and the flow was continued until the product was taken out after 8 days. After cooling the furnace, the packing coke was removed, the graphite case was taken out, and the carbon fiber molded body inside was taken out.

【0014】得られた炭素繊維成型体は一部に媒状の炭
素が付着していた以外には外観状の異状は認められず、
酸化消耗もほとんど認められなかった。また黒鉛化収縮
により成型体厚さが平均1.8%減じたが、反り、変形
等はなかった。成型体の灰分は平均287ppmであっ
た。
The obtained carbon fiber molded body showed no abnormal appearance except that a part of carbon-like carbon was adhered to it.
Almost no oxidative consumption was observed. Further, the thickness of the molded body was reduced by an average of 1.8% due to graphitization shrinkage, but there was no warpage or deformation. The ash content of the molded body was 287 ppm on average.

【0015】[0015]

【比較例1】実施例1と同様にして得た1500×10
00mm、厚さ52mm、平均密度0.196g/cm
3の低密度炭素繊維成型体6枚を、1500×1000
mm、厚さ40mmの黒鉛板2枚で両側から狭み込む形
で図6の様にアチソン炉内に設置した。周囲は押出材炭
素板等7の製品を配置した。全体をパッキングコークス
内に埋めた後、常法に従って通電加熱し、冷却後成型体
8を取り出した。成型体のX回線折指数(d002)よ
り推定した熱処理温度は2550℃であった。得られた
成型体は厚さが平均5.6%減した他、パッキングコー
クスに接している部分は著しく酸化消耗しており、部分
的には200mm程内部まで浸食されていた。また灰分
は平均1230ppmであった(9:黒鉛板)。
Comparative Example 1 1500 × 10 obtained in the same manner as in Example 1
00 mm, thickness 52 mm, average density 0.196 g / cm
Six low density carbon fiber moldings of 3 , 1500 x 1000
It was installed in the Acheson furnace as shown in FIG. 6 in such a manner that two graphite plates having a thickness of 40 mm and a thickness of 40 mm were sandwiched from both sides. 7 products such as extruded carbon plates were arranged around the product. After the whole was embedded in a packing coke, it was electrically heated according to a conventional method, and after cooling, the molded body 8 was taken out. The heat treatment temperature estimated from the X-ray bending index (d00 2 ) of the molded product was 2550 ° C. In the obtained molded body, the thickness was reduced by 5.6% on average, and the portion in contact with the packing coke was remarkably oxidized and consumed, and the inner portion was partially eroded by about 200 mm. The ash content was 1230 ppm on average (9: graphite plate).

【0016】[0016]

【発明の効果】本発明により、変形等を生じにくい、生
産性、品質等に優れた低密度炭素繊維成型体の黒鉛化処
理方法を提供しうる。
EFFECTS OF THE INVENTION The present invention can provide a method for graphitizing a low-density carbon fiber molded body which is resistant to deformation and is excellent in productivity and quality.

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

【図1】 図1は本発明に用いる黒鉛材製の容器の説
明図である。
FIG. 1 is an explanatory view of a container made of a graphite material used in the present invention.

【図2】 図2は本発明に用いる黒鉛材製の容器の説
明図である。
FIG. 2 is an explanatory view of a container made of a graphite material used in the present invention.

【図3】 図3は本発明方法をアチソン炉を用いて実
施している状態を示す説明図である。
FIG. 3 is an explanatory view showing a state where the method of the present invention is carried out using an Atchison furnace.

【図4】 図4は本発明方法をアチソン炉を用いて実
施している状態を通電方向に直交する断面で切った説明
図である。
FIG. 4 is an explanatory view showing a state in which the method of the present invention is carried out using an Acheson furnace, which is cut along a cross section orthogonal to the current-carrying direction.

【図5】 図5は本発明の実施例において用いたアチ
ソン炉の状態(炉上面方向及び炉断面方向からみた状
態)を示す説明図である。
FIG. 5 is an explanatory view showing a state of the Acheson furnace used in the examples of the present invention (a state viewed from the furnace top surface direction and the furnace cross-sectional direction).

【図6】 図6は本発明の実施例において用いたアチ
ソン炉の状態を示す説明図である。
FIG. 6 is an explanatory view showing the state of the Acheson furnace used in the examples of the present invention.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 八十島 亮 山梨県中巨摩群櫛形町小笠原1226−1番地 東洋カーボン株式会社山梨工場内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Ryo Yashima Shima 122-1 Ogasawara, Kushigata-cho, Nakakoma-gun, Yamanashi Toyo Carbon Co., Ltd. Yamanashi factory

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 密度1.0g/cm3以下の炭素繊維
成型体を黒鉛材製の容器に収め、パッキングコークス中
に埋め込んで、その後黒鉛化処理することを特徴とする
低密度炭素繊維成形体の黒鉛化処理方法。
1. A low-density carbon fiber molded product characterized by containing a carbon fiber molded product having a density of 1.0 g / cm 3 or less in a container made of a graphite material, embedding it in packing coke, and then subjecting it to graphitization treatment. Graphitization treatment method.
JP3343662A 1991-12-25 1991-12-25 Method for graphitizing low-density carbon fiber moldings Expired - Lifetime JP3042554B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3343662A JP3042554B2 (en) 1991-12-25 1991-12-25 Method for graphitizing low-density carbon fiber moldings

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3343662A JP3042554B2 (en) 1991-12-25 1991-12-25 Method for graphitizing low-density carbon fiber moldings

Publications (2)

Publication Number Publication Date
JPH07252726A true JPH07252726A (en) 1995-10-03
JP3042554B2 JP3042554B2 (en) 2000-05-15

Family

ID=18363272

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3343662A Expired - Lifetime JP3042554B2 (en) 1991-12-25 1991-12-25 Method for graphitizing low-density carbon fiber moldings

Country Status (1)

Country Link
JP (1) JP3042554B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013058348A1 (en) * 2011-10-21 2013-04-25 昭和電工株式会社 Method for producing electrode material for lithium ion batteries
WO2013058347A1 (en) * 2011-10-21 2013-04-25 昭和電工株式会社 Method for producing electrode material for lithium ion batteries

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013058348A1 (en) * 2011-10-21 2013-04-25 昭和電工株式会社 Method for producing electrode material for lithium ion batteries
WO2013058347A1 (en) * 2011-10-21 2013-04-25 昭和電工株式会社 Method for producing electrode material for lithium ion batteries
JP5401632B2 (en) * 2011-10-21 2014-01-29 昭和電工株式会社 Method for producing electrode material for lithium ion battery
JP5401631B2 (en) * 2011-10-21 2014-01-29 昭和電工株式会社 Method for producing electrode material for lithium ion battery
JP2014029874A (en) * 2011-10-21 2014-02-13 Showa Denko Kk Manufacturing method of graphite material for lithium ion battery electrode material
JP2014053314A (en) * 2011-10-21 2014-03-20 Showa Denko Kk Method for producing graphite material for lithium ion battery electrode material
JPWO2013058348A1 (en) * 2011-10-21 2015-04-02 昭和電工株式会社 Method for producing electrode material for lithium ion battery
JPWO2013058347A1 (en) * 2011-10-21 2015-04-02 昭和電工株式会社 Method for producing electrode material for lithium ion battery
US9059467B2 (en) 2011-10-21 2015-06-16 Showa Denko K.K. Method for producing electrode material for lithium ion batteries
US9284192B2 (en) 2011-10-21 2016-03-15 Showa Denko K.K. Method for producing electrode material for lithium ion batteries

Also Published As

Publication number Publication date
JP3042554B2 (en) 2000-05-15

Similar Documents

Publication Publication Date Title
US5038019A (en) High temperature diffusion furnace
ES2215022T3 (en) GRAPHITE CATTOP IMPREGNATED FOR THE ELECTROLYSIS OF ALUMINUM.
JPH07252726A (en) Method for graphitization of low-density carbon fiber molded form
KR101554912B1 (en) Method for preparing graphite and furnace therefor
US6783747B1 (en) Graphite carbon powder, and method and apparatus for producing the same
US6627062B1 (en) Graphite cathode for the electrolysis of aluminium
US702758A (en) Method of graphitizing electrodes.
US2213073A (en) Furnace electrode
JP4782537B2 (en) Carbon material firing furnace and carbon material firing method
JP3838618B2 (en) Graphite carbon powder, production method and apparatus thereof
JPS6311448B2 (en)
JP2006306724A (en) Graphite carbon powder and method and apparatus for producing the same
JPH03330B2 (en)
US1997622A (en) Electric furnace and method of operating the same
JPH09227232A (en) Graphitization method for carbonaceous molding
JPS5849483B2 (en) Cathode carbon block manufacturing method for aluminum electrolyzer
EP0225549B1 (en) Electrically conductive brick
JPH0753623B2 (en) Method for forming a silicon carbide film on the surface of a graphite electrode along with graphitization
JPH0238548B2 (en)
US345860A (en) Apparatus for carbonizing fiber
SU1046976A2 (en) Resistive electric heater for furnaces
US1306251A (en) colby
JPS58106384A (en) Heating furnace
JP2717848B2 (en) Graphitization of fired carbon electrode
JPS61143687A (en) High-temperature electric furnace

Legal Events

Date Code Title Description
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090310

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090310

Year of fee payment: 9

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090310

Year of fee payment: 9

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090310

Year of fee payment: 9

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313115

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090310

Year of fee payment: 9

R360 Written notification for declining of transfer of rights

Free format text: JAPANESE INTERMEDIATE CODE: R360

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090310

Year of fee payment: 9

R360 Written notification for declining of transfer of rights

Free format text: JAPANESE INTERMEDIATE CODE: R360

R371 Transfer withdrawn

Free format text: JAPANESE INTERMEDIATE CODE: R371

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090310

Year of fee payment: 9

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313115

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090310

Year of fee payment: 9

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090310

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100310

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100310

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110310

Year of fee payment: 11

EXPY Cancellation because of completion of term
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120310

Year of fee payment: 12