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JP4096402B2 - Graphitization furnace - Google Patents
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JP4096402B2 - Graphitization furnace - Google Patents

Graphitization furnace Download PDF

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Publication number
JP4096402B2
JP4096402B2 JP12251298A JP12251298A JP4096402B2 JP 4096402 B2 JP4096402 B2 JP 4096402B2 JP 12251298 A JP12251298 A JP 12251298A JP 12251298 A JP12251298 A JP 12251298A JP 4096402 B2 JP4096402 B2 JP 4096402B2
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Japan
Prior art keywords
graphite
hopper
graphitization furnace
gas
carbon powder
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JP12251298A
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Japanese (ja)
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JPH11314909A (en
Inventor
重樹 飯島
清 根橋
至康 松田
賢一 西
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IHI Corp
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IHI Corp
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Description

【0001】
【発明の属する技術分野】
本発明は、黒鉛粉末を製造する黒鉛化炉に関するものである。
【0002】
【従来の技術】
従来、炭素粉粒体を、無酸化雰囲気下(たとえば真空下や不活性雰囲気下)で約3100℃以上に加熱処理することにより、前記炭素粉粒体を黒鉛化して工業的に黒鉛粉末を製造することが行なわれている。
【0003】
そして、この黒鉛粉末の製造には、アチソン炉等の黒鉛化電気炉が用いられ、バッチ式の加熱処理により黒鉛粉末を製造するようにしているが、これを連続的に行なうことのできる黒鉛化炉の開発が望まれている。
【0004】
【発明が解決しようとする課題】
このような連続処理を行なうには、炉本体に連続的に炭素粉粒体を供給するとともに加熱処理後に生成される黒鉛を炉本体から連続的に排出しなければならない。しかも、炭素粉粒体の連続加熱処理を行なうためには、前記炉本体の内部を無酸化雰囲気下に保持する必要がある。しかしながら、投入される炭素粉粒体が外気を含んでおり、この炭素粉粒体を前記炉本体に投入する際に、この炭素粉粒体とともに外気が炉本体内に侵入し、また、生成された黒鉛を炉本体から外部へ排出する際に、その排出孔から外気が炉本体内に侵入して、炉本体内部の無酸化雰囲気が破壊されてしまうことが想定されることから、その対策が必要である。
【0005】
一方、このような不具合を解消するために、炭素粉粒体の搬送装置や黒鉛の排出装置を含めた黒鉛化炉全体が設置される建屋内全体を無酸化雰囲気とすることが考えられるが、装置が大掛かりとなり、この結果、設備コストの高騰を招いてしまい実用的ではない。
【0006】
本発明は、このような諸問題点に鑑みてなされたものであり、設備コストの高騰を抑制しつつ、炉本体内の無酸化状態を破壊することなく炭素粉粒体の装入を連続して行ない、または、生成された黒鉛の排出を連続して行なうことのできる黒鉛化炉を提供することを目的とする。
【0007】
【課題を解決するための手段】
上述の目的を達成するために、第1の黒鉛化炉は、黒鉛化炉本体と、該黒鉛化炉本体に炭素粉粒体を投入する原料投入装置とを備え、前記原料投入装置が、前記炭素粉粒体が投入される受け入れホッパと、該受け入れホッパから前記炭素粉粒体の供給を受けるとともに該炭素粉粒体まわりの空気を無酸化ガスと置換する無酸化ガス置換手段と、該無酸化ガス置換手段から前記炭素粉粒体の供給を受けるとともに該炭素粉粒体を前記黒鉛化炉本体へ所定量ずつ供給する装入手段とを備えて構成され、前記受け入れホッパと前記無酸化ガス置換手段との間、および前記無酸化ガス置換手段と装入手段との間には、炭素粉粒体の流動経路を遮断する開閉機構が設けられることを特徴とする。
【0008】
また、第2の黒鉛化炉は、黒鉛化炉本体と、該黒鉛化炉において生成された黒鉛を排出する黒鉛排出装置とを備え、前記黒鉛排出装置が、前記黒鉛を黒鉛化炉本体から排出される黒鉛を貯留するとともに該黒鉛まわりの雰囲気を外気と置換する外気置換手段を備えて構成され、該外気置換手段と前記黒鉛化炉本体との間、および前記外気置換手段に設けられた黒鉛排出部には、黒鉛の流動経路を遮断する開閉機構が設けられることを特徴とする。
【0009】
【発明の実施の形態】
以下、本発明の一実施形態を図1ないし図5を参照して説明する。
図1において符号1は水冷構造とした黒鉛化炉本体(以下、炉本体と称す)を示している。この炉本体1の上部には、原料となる炭素粉粒体を投入する原料投入装置2が設けられている。
【0010】
この原料投入装置2は、炭素粉粒体が投入される受け入れホッパ3と、受け入れホッパ3から炭素粉粒体の供給を受けるとともに炭素粉粒体まわりの空気を無酸化ガスと置換する無酸化ガス置換手段4と、無酸化ガス置換手段4から炭素粉粒体の供給を受けるとともに炭素粉粒体を炉本体1へ所定量ずつ供給する装入手段5とから構成されている。ここで、無酸化ガスとは炭素紛粒体の酸化を抑制する気体である。
【0011】
受け入れホッパ3と無酸化ガス置換手段4との間、および無酸化ガス置換手段4と装入手段5との間には、炭素粉粒体の流動経路を遮断する開閉機構6が設けられている。
【0012】
炉本体1には、対となる電極7,8が装着されており、炉本体1内に充填される炭素粉粒体へ通電して、ジュール熱によって炭素粉粒体を加熱処理するようになっている。
【0013】
受け入れホッパ3の下部には、図2に示すように、開閉機構6としての遮蔽弁が連設されているとともに、その下方には、開閉機構6が開放状態にある場合に作動させられて、受け入れホッパ3内の炭素粉粒体を、順次、下方の無酸化ガス置換手段4へ送り込むロータリバルブ9が連設されている。
【0014】
無酸化ガス置換手段4は、ロータリバルブ9から供給される炭素粉粒体を受け入れる空気ガス置換ホッパ10と、この空気ガス置換ホッパ10に無酸化ガスを供給する無酸化ガス供給管11と、空気ガス置換ホッパ10の内部気体を外部へ導く排気管12と、無酸化ガス供給管11および排気管12のそれぞれに設けられた遮蔽弁13,14と、排気管12の、遮蔽弁14よりも下流側に設けられ、空気ガス置換ホッパ10の内部気体を外部へ排出する排気ポンプ15とによって構成されている。
【0015】
また、空気ガス置換ホッパ10の下部には、開閉機構6としての遮蔽弁が連設されているとともに、その下方には、開閉機構6が開放状態にある場合に作動させられて、空気ガス置換ホッパ10内の炭素粉粒体を、順次、下方の装入手段5へ送り込むロータリバルブ16が連設されている。
【0016】
さらに、装入手段5は、ロータリバルブ16から供給される炭素粉粒体を受け入れる装入ホッパ17と、この装入ホッパ17にロータリバルブ18を介して連設されたスクリューフィーダ19とによって構成されており、装入ホッパ17内の炭素粉粒体が、ロータリバルブ18によって順次切り出されてスクリューフィーダ19へ供給されるとともに、このスクリューフィーダ19によって炉本体1へ装入されるようになっている。
【0017】
一方、本実施形態においては、炉本体1には、図1に示すように、加熱処理後に生成された黒鉛を炉本体1の外部へ排出する黒鉛排出管20が、炉本体1の内部中央から炉本体1の外部下方に突出して設けられており、この黒鉛排出管20の下端部に、この黒鉛排出管20を流下させられる黒鉛を切り出して外部へ排出する切り出しホッパ21が連設されている。
【0018】
この切り出しホッパ21の内部には、黒鉛排出管20の下端に対向して配設されるとともに、駆動機構22によって水平回転させられるターンテーブル23と、このターンテーブル23の回転に伴い、このターンテーブル23上に切り出された黒鉛を下方へ落下させるスクレーパ24とが設けられ、また、切り出しホッパ21の下部には、スクレーパ24によって落下させられた黒鉛を受け止める集積部材25と、この集積部材25の下方に連設されて集積された黒鉛の落下およびその停止を行なう遮蔽弁26と、この遮蔽弁26の下方に連設され、この遮蔽弁26を経て落下させられる黒鉛を一旦貯留するとともに、この黒鉛回りを外気と同様の雰囲気とする外気置換手段としてのガス空気置換ホッパ27と、このガス空気置換ホッパ27の下方に連設され、ガス空気置換ホッパ27から黒鉛を外部に排出する遮蔽弁28とが連設されている。
【0019】
図3に示すように、集積部材25の下方に設けられた遮蔽弁26の下方には、この遮蔽弁26が開放された状態において作動させられて、集積部材25内の黒鉛をガス空気置換ホッパ27へ送り込むためのロータリバルブ29が設けられ、また、ガス空気置換ホッパ27の下方に設けられた遮蔽弁28の下方には、遮蔽弁28が開放された状態において作動させられて、ガス空気置換ホッパ27内の黒鉛を外部へ排出するロータリバルブ30が設けられて折り、これらによって、本実施形態における黒鉛排出装置が構成されている。
【0020】
さらに、ガス空気置換ホッパ27には、外気導入管31と排気管32が連設されており、これらの外気導入管31および排気管32には遮蔽弁33,34がそれぞれ設けられているとともに、排気管32には排気ポンプ35が設けられ、ガス空気置換ホッパ27の上部に設けられている遮蔽弁26および下方に設けられている遮蔽弁28が閉塞された状態において、両遮蔽弁33,34が開放されるとともに排気ポンプ35が作動させられることにより、ガス空気置換ホッパ27内の無酸化ガスが外気によって置換されるとともに、この外気によってガス空気置換ホッパ27内の黒鉛が所定温度まで冷却されるようになっている。
【0021】
このように構成された本実施形態に係わる黒鉛化炉においては、受け入れホッパ3に原料となる炭素粉粒体が投入されて一旦貯留された後に、空気ガス置換ホッパ10へ供給されるが、この空気ガス置換ホッパ10内に所定量の炭素粉粒体が供給されると、ロータリバルブ9の作動が停止されるとともに、開閉機構6が閉塞される。
【0022】
このとき、空気ガス置換ホッパ10の下方に設けられている開閉機構6およびロータリバルブ16も停止させられており、これによって、空気ガス置換ホッパ10内に炭素粉粒体が貯留される。
この状態において、遮蔽弁13および遮蔽弁14が開放されるとともに、排気ポンプ15が作動させられることにより、空気ガス置換ホッパ10内の気体が外部へ排出され、かつ、空気ガス置換ホッパ10内に、図示せぬチャンバから無酸化ガス供給管11を経て無酸化ガスが供給され、これによって、空気ガス置換ホッパ10内の炭素粉粒体回りが無酸化雰囲気となされる。
【0023】
そして、装入ホッパ17内の炭素粉粒体の貯留量が所定量以下となった時点で、開閉機構6が開放されるとともにロータリバルブ16が作動させられることにより、空気ガス置換ホッパ10内の炭素粉粒体が無酸化雰囲気のまま装入ホッパ17へ供給される。
【0024】
このように装入ホッパ17への炭素粉粒体の供給が行なわれている間においても、ロータリバルブ18およびスクリューフィーダ19による炉本体1への炭素粉粒体の供給は継続して行なわれている。
【0025】
ここで、受け入れホッパ3への原料の投入時期や投入量、また、この受け入れホッパ3から空気ガス置換ホッパ10への炭素粉粒体の供給時期や供給量を、装入ホッパ17から連続して行なわれている炭素粉粒体の供給量に合わせて調整することにより、炉本体1への炭素粉粒体の供給が途切れることなく連続して均一に行なわれるとともに、空気ガス置換ホッパ10における置換操作によって、炭素粉粒体とともに外気が装入ホッパ17へ侵入してしまうようなことがなく、また、生成された黒鉛の排出時においても、ガス空気置換ホッパ27およびその上流部と下流部における遮蔽弁26,27の作用によって外気が炉本体1へ侵入することが防止される。
【0026】
一方、炉本体1における熱処理によって生成された黒鉛は、黒鉛排出管20を経て順次切り出しホッパ21へ排出されてターンテーブル23から集積部材25を経てガス空気置換ホッパ27内に落下、貯留させられ、このガス空気置換ホッパ27内に所定量の黒鉛が貯留させられた時点で、ガス置換ホッパ27の上方に設けられている遮蔽弁26が閉じられるとともに、図示せぬチャンバからガス置換ホッパ27内に外気が導入され、この外気導入が十分に行なわれ、黒鉛が十分に冷却された後に、ガス置換ホッパ27の下方に設けられている遮蔽弁28が開放されることにより、生成された黒鉛が外部へ排出される。
【0027】
このように本実施形態においては、炉本体1内への外気の侵入が確実に防止された状態で黒鉛化処理が連続して行なわれる。
【0028】
なお、前述した実施形態において装入手段5にスクリューフィーダ19を用いた例について示したが、これに代えて、図4に示すように、コンベア36を用いてもよい。また、図5に示すように、ターンテーブル37を用いてもよい。
【0029】
【発明の効果】
以上説明したように、本発明の黒鉛化炉によれば、原料の炭素粉粒体を炉本体に供給する場合または生成された黒鉛を外部へ排出する場合において、外部の空気が炉本体に侵入することを防止しつつ、原料の連続供給ならびにこの原料の連続加熱処理および生成された黒鉛の連続排出を行なうことができる。しかも、大掛かりな処理装置を必要としないので、設備コストの高騰を抑制することができる。
【図面の簡単な説明】
【図1】 本発明の一実施形態を示す黒鉛化炉の全体図である。
【図2】 図1における原料投入部の概略構成図である。
【図3】 図1における黒鉛排出部の概略構成図である。
【図4】 本発明の装入手段の変形例を示す正面図である。
【図5】 本発明の装入手段の他の変形例を示す正面図である。
【符号の説明】
1 炉本体
2 原料投入装置
3 受け入れホッパ
4 無酸化ガス置換手段
5 装入手段
6 開閉機構
20 黒鉛排出管(黒鉛排出装置)
21 切り出しホッパ(黒鉛排出装置)
23 ターンテーブル(黒鉛排出装置)
26 遮蔽弁(開閉機構)
28 遮蔽弁(開閉機構)
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a graphitization furnace for producing graphite powder.
[0002]
[Prior art]
Conventionally, carbon powder particles are heat-treated at about 3100 ° C. or higher in a non-oxidizing atmosphere (for example, in a vacuum or an inert atmosphere), thereby graphitizing the carbon particles to industrially produce graphite powder. To be done.
[0003]
And, for the production of this graphite powder, a graphitization electric furnace such as an Atchison furnace is used, and the graphite powder is produced by batch-type heat treatment, but the graphitization can be carried out continuously. Development of a furnace is desired.
[0004]
[Problems to be solved by the invention]
In order to perform such a continuous process, it is necessary to continuously supply carbon powder particles to the furnace body and continuously discharge graphite generated after the heat treatment from the furnace body. Moreover, in order to perform the continuous heat treatment of the carbon powder particles, it is necessary to keep the inside of the furnace body in a non-oxidizing atmosphere. However, the carbon particles to be charged contain outside air, and when the carbon particles are charged into the furnace body, the outside air enters the furnace body together with the carbon particles and is generated. When exhausting graphite from the furnace body to the outside, it is assumed that outside air will enter the furnace body from the discharge hole and the non-oxidizing atmosphere inside the furnace body will be destroyed. is necessary.
[0005]
On the other hand, in order to eliminate such problems, it is conceivable that the entire building where the entire graphitization furnace including the carbon particle conveyance device and the graphite discharge device is installed has a non-oxidizing atmosphere. The apparatus becomes large, and as a result, the equipment cost increases, which is not practical.
[0006]
The present invention has been made in view of such various problems, and it is possible to continuously charge carbon particles without destroying the non-oxidation state in the furnace body while suppressing the increase in equipment cost. It is an object of the present invention to provide a graphitization furnace capable of continuously performing or discharging the produced graphite.
[0007]
[Means for Solving the Problems]
In order to achieve the above-mentioned object, the first graphitization furnace includes a graphitization furnace main body and a raw material input device that inputs carbon powder particles into the graphitization furnace main body, and the raw material input device includes: A receiving hopper into which carbon powder particles are charged, non-oxidizing gas replacement means for receiving supply of the carbon powder particles from the receiving hopper and replacing air around the carbon powder particles with non-oxidizing gas; The receiving hopper and the non-oxidizing gas are configured to include supply means for receiving the carbon powder particles from the oxidizing gas replacement means and supplying the carbon powder particles to the graphitization furnace main body by a predetermined amount. An opening / closing mechanism for blocking the flow path of the carbon powder is provided between the replacement means and between the non-oxidizing gas replacement means and the charging means.
[0008]
The second graphitization furnace includes a graphitization furnace main body and a graphite discharge device for discharging the graphite generated in the graphitization furnace, and the graphite discharge device discharges the graphite from the graphitization furnace main body. And is provided with outside air replacement means for storing the atmosphere of graphite and replacing the atmosphere around the graphite with outside air, and is provided between the outside air replacement means and the graphitization furnace main body and the graphite provided in the outside air replacement means. The discharge part is provided with an opening / closing mechanism for blocking a flow path of graphite.
[0009]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, an embodiment of the present invention will be described with reference to FIGS.
In FIG. 1, the code | symbol 1 has shown the graphitization furnace main body (henceforth a furnace main body) made into the water cooling structure. At the upper part of the furnace body 1, a raw material charging device 2 for charging carbon powder as a raw material is provided.
[0010]
The raw material charging apparatus 2 includes a receiving hopper 3 into which carbon powder particles are charged, and a non-oxidizing gas that receives the supply of carbon powder particles from the receiving hopper 3 and replaces air around the carbon powder particles with a non-oxidizing gas. The replacement means 4 and the charging means 5 that receives the supply of carbon particles from the non-oxidizing gas replacement means 4 and supplies the carbon particles to the furnace body 1 by a predetermined amount. Here, the non-oxidizing gas is a gas that suppresses oxidation of the carbon powder particles.
[0011]
Between the receiving hopper 3 and the non-oxidizing gas replacement means 4 and between the non-oxidizing gas replacement means 4 and the charging means 5, an opening / closing mechanism 6 for blocking the flow path of the carbon powder is provided. .
[0012]
The furnace body 1 is equipped with a pair of electrodes 7 and 8. The carbon powder filled in the furnace body 1 is energized and the carbon powder is heated by Joule heat. ing.
[0013]
As shown in FIG. 2, a shielding valve as an opening / closing mechanism 6 is connected to the lower portion of the receiving hopper 3, and below that, when the opening / closing mechanism 6 is in an open state, it is operated. A rotary valve 9 for sequentially feeding the carbon powder particles in the receiving hopper 3 to the lower non-oxidizing gas replacement means 4 is continuously provided.
[0014]
The non-oxidizing gas replacement means 4 includes an air gas replacement hopper 10 that receives carbon powder supplied from the rotary valve 9, a non-oxidizing gas supply pipe 11 that supplies non-oxidizing gas to the air gas replacement hopper 10, and air The exhaust pipe 12 that guides the internal gas of the gas replacement hopper 10 to the outside, shielding valves 13 and 14 provided in the non-oxidizing gas supply pipe 11 and the exhaust pipe 12, and the exhaust pipe 12 downstream of the shielding valve 14. And an exhaust pump 15 that discharges the internal gas of the air gas replacement hopper 10 to the outside.
[0015]
In addition, a shielding valve as the opening / closing mechanism 6 is connected to the lower part of the air gas replacement hopper 10, and the air gas replacement is operated below the opening / closing mechanism 6 when the opening / closing mechanism 6 is in an open state. A rotary valve 16 for sequentially feeding the carbon powder particles in the hopper 10 to the lower charging means 5 is connected.
[0016]
Further, the charging means 5 is constituted by a charging hopper 17 that receives the carbon powder supplied from the rotary valve 16 and a screw feeder 19 that is connected to the charging hopper 17 via the rotary valve 18. The carbon powder particles in the charging hopper 17 are sequentially cut out by the rotary valve 18 and supplied to the screw feeder 19, and the screw feeder 19 is charged into the furnace body 1. .
[0017]
On the other hand, in the present embodiment, as shown in FIG. 1, the furnace body 1 has a graphite discharge pipe 20 that discharges the graphite generated after the heat treatment to the outside of the furnace body 1 from the inner center of the furnace body 1. A cut-out hopper 21 that cuts out the graphite that is allowed to flow down the graphite discharge pipe 20 and discharges it to the outside is provided at the lower end portion of the graphite discharge pipe 20 so as to protrude downward from the furnace body 1. .
[0018]
Inside the cut-out hopper 21, the turntable 23 is disposed opposite to the lower end of the graphite discharge pipe 20 and is horizontally rotated by the drive mechanism 22, and the turntable 23 is rotated along with the rotation of the turntable 23. A scraper 24 for dropping the graphite cut out on the scraper 24 is provided, and an accumulation member 25 for receiving the graphite dropped by the scraper 24 and a lower portion of the accumulation member 25 are provided below the cutting hopper 21. A shield valve 26 that drops and stops the graphite that is continuously provided and accumulated, and a graphite that is continuously provided below the shield valve 26 and is dropped through the shield valve 26, and temporarily stores the graphite. A gas / air replacement hopper 27 serving as an outside air replacement means for making the atmosphere similar to the outside air, and the gas / air replacement hopper 27 Is continuously provided downward, it is shielded valve 28 are communicated set to discharge the graphite to the outside from the gas air displacement hopper 27.
[0019]
As shown in FIG. 3, below the shielding valve 26 provided below the accumulating member 25, the shielding valve 26 is operated in an open state, and the graphite in the accumulating member 25 is replaced with a gas-air replacement hopper. A rotary valve 29 for feeding the gas to the air 27 is provided, and a gas / air replacement is performed below the shielding valve 28 provided below the gas / air replacement hopper 27 with the shielding valve 28 opened. A rotary valve 30 for discharging the graphite in the hopper 27 to the outside is provided and folded, and these constitute the graphite discharging apparatus in the present embodiment.
[0020]
Further, the gas-air replacement hopper 27 is provided with an outside air introduction pipe 31 and an exhaust pipe 32, and the outside air introduction pipe 31 and the exhaust pipe 32 are provided with shielding valves 33 and 34, respectively. The exhaust pipe 32 is provided with an exhaust pump 35. In a state where the shielding valve 26 provided at the upper part of the gas-air replacement hopper 27 and the shielding valve 28 provided below are closed, both shielding valves 33, 34 are provided. Is opened and the exhaust pump 35 is operated, so that the non-oxidizing gas in the gas-air replacement hopper 27 is replaced by the outside air, and the graphite in the gas-air replacement hopper 27 is cooled to a predetermined temperature by the outside air. It has become so.
[0021]
In the graphitization furnace according to the present embodiment configured as described above, the carbon powder as a raw material is charged into the receiving hopper 3 and temporarily stored, and then supplied to the air gas replacement hopper 10. When a predetermined amount of carbon powder is supplied into the air gas replacement hopper 10, the operation of the rotary valve 9 is stopped and the opening / closing mechanism 6 is closed.
[0022]
At this time, the opening / closing mechanism 6 and the rotary valve 16 provided below the air gas replacement hopper 10 are also stopped, whereby the carbon powder particles are stored in the air gas replacement hopper 10.
In this state, when the shielding valve 13 and the shielding valve 14 are opened and the exhaust pump 15 is operated, the gas in the air gas replacement hopper 10 is discharged to the outside, and the air gas replacement hopper 10 The non-oxidizing gas is supplied from the chamber (not shown) through the non-oxidizing gas supply pipe 11, and thereby, the surroundings of the carbon powder particles in the air gas replacement hopper 10 are made into the non-oxidizing atmosphere.
[0023]
And when the storage amount of the carbon powder particles in the charging hopper 17 becomes equal to or less than a predetermined amount, the opening / closing mechanism 6 is opened and the rotary valve 16 is operated, whereby the air gas replacement hopper 10 The carbon powder particles are supplied to the charging hopper 17 in a non-oxidizing atmosphere.
[0024]
In this way, even while the carbon particles are being supplied to the charging hopper 17, the carbon particles are continuously supplied to the furnace body 1 by the rotary valve 18 and the screw feeder 19. Yes.
[0025]
Here, the charging timing and the charging amount of the raw material to the receiving hopper 3 and the supplying timing and supplying amount of the carbon powder particles from the receiving hopper 3 to the air gas replacement hopper 10 are continuously supplied from the charging hopper 17. By adjusting according to the supply amount of the carbon powder being performed, the supply of the carbon powder to the furnace body 1 is performed continuously without interruption, and the replacement in the air gas replacement hopper 10 is performed. The operation prevents the outside air from entering the charging hopper 17 together with the carbon powder particles, and also at the time of discharging the generated graphite, the gas-air replacement hopper 27 and the upstream and downstream portions thereof. The action of the shielding valves 26 and 27 prevents outside air from entering the furnace body 1.
[0026]
On the other hand, the graphite generated by the heat treatment in the furnace body 1 is sequentially cut out through the graphite discharge pipe 20 and discharged into the hopper 21 and dropped and stored in the gas-air replacement hopper 27 through the accumulation member 25 from the turntable 23. When a predetermined amount of graphite is stored in the gas / air replacement hopper 27, the shielding valve 26 provided above the gas replacement hopper 27 is closed and the chamber (not shown) enters the gas replacement hopper 27. After the outside air is introduced, the introduction of the outside air is sufficiently performed, and the graphite is sufficiently cooled. Then, the shielding valve 28 provided below the gas replacement hopper 27 is opened, so that the produced graphite is outside. Is discharged.
[0027]
Thus, in the present embodiment, the graphitization process is continuously performed in a state in which the intrusion of outside air into the furnace body 1 is reliably prevented.
[0028]
In the embodiment described above, an example in which the screw feeder 19 is used for the charging means 5 has been described. However, instead of this, a conveyor 36 may be used as shown in FIG. Further, a turntable 37 may be used as shown in FIG.
[0029]
【The invention's effect】
As described above, according to the graphitization furnace of the present invention, when supplying the raw carbon particles to the furnace body or when discharging the generated graphite to the outside, external air enters the furnace body. The raw material can be continuously supplied, the raw material can be continuously heated, and the generated graphite can be continuously discharged. In addition, since a large-scale processing apparatus is not required, an increase in equipment cost can be suppressed.
[Brief description of the drawings]
FIG. 1 is an overall view of a graphitization furnace showing an embodiment of the present invention.
FIG. 2 is a schematic configuration diagram of a raw material charging unit in FIG.
FIG. 3 is a schematic configuration diagram of a graphite discharge unit in FIG. 1;
FIG. 4 is a front view showing a modification of the charging means of the present invention.
FIG. 5 is a front view showing another modification of the charging means of the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Furnace body 2 Raw material charging device 3 Receiving hopper 4 Non-oxidizing gas replacement means 5 Loading means 6 Opening / closing mechanism 20 Graphite discharge pipe (graphite discharge apparatus)
21 Cutting hopper (graphite discharge device)
23 Turntable (graphite discharge device)
26 Shielding valve (opening / closing mechanism)
28 Shielding valve (open / close mechanism)

Claims (2)

黒鉛化炉本体と、該黒鉛化炉本体に炭素粉粒体を投入する原料投入装置と、前記黒鉛化炉本体において生成された黒鉛を排出する黒鉛排出装置とを備えた黒鉛化炉であって、
前記原料投入装置が、前記炭素粉粒体が投入される受け入れホッパと、該受け入れホッパから前記炭素粉粒体の供給を受けるとともに該炭素粉粒体まわりの空気を無酸化ガスと置換する無酸化ガス置換手段と、該無酸化ガス置換手段から前記炭素粉粒体の供給を受けるとともに該炭素粉粒体を前記黒鉛化炉本体へ所定量ずつ供給する装入手段とを備えて構成され、
前記受け入れホッパと前記無酸化ガス置換手段との間、および前記無酸化ガス置換手段と装入手段との間には、炭素粉粒体の流動経路を遮断する開閉機構が設けられ、
前記黒鉛排出装置が、
前記黒鉛化炉本体の内部中央から当該黒鉛化炉本体の外部下方に突出して設けられた黒鉛排出管と、
該黒鉛排出管の下端部に設けられ、当該黒鉛排出管を流下する黒鉛を切り出して外部へ排出する切り出しホッパと、
該切り出しホッパの内部に設けられ、前記黒鉛排出管の下端に対向して配設されるとともに水平回転するターンテーブルと、
前記切り出しホッパの内部に設けられ、前記ターンテーブルの回転に伴い、当該ターンテーブル上に切り出された黒鉛を下方へ落下させるスクレーパと、
前記切り出しホッパの内部に設けられ、前記スクレーパによって落下させられた黒鉛を受け止める集積部材と、
該集積部材の下方に連設されて集積された黒鉛の落下およびその停止を行なう遮蔽弁と、
該遮蔽弁の下方に連設され、当該遮蔽弁を経て落下させられる黒鉛を一旦貯留するとともに、この黒鉛回りを外気と同様の雰囲気とするガス空気置換ホッパと、
該ガス空気置換ホッパの下方に連設され、当該ガス空気置換ホッパから黒鉛を外部に排出する遮蔽弁とを備えることを特徴とする黒鉛化炉。
A graphitization furnace comprising: a graphitization furnace main body; a raw material input device that inputs carbon powder into the graphitization furnace main body; and a graphite discharge device that discharges graphite generated in the graphitization furnace main body. ,
The raw material charging device receives a receiving hopper into which the carbon powder particles are charged, and receives the supply of the carbon powder particles from the receiving hopper and replaces the air around the carbon powder particles with a non-oxidizing gas. Gas replacement means, and charging means for receiving the carbon powder particles from the non-oxidizing gas replacement means and supplying the carbon powder particles to the graphitization furnace main body by a predetermined amount.
Between the receiving hopper and the non-oxidizing gas replacement means, and between the non-oxidizing gas replacement means and the charging means, an opening / closing mechanism for blocking the flow path of the carbon powder is provided,
The graphite discharge device,
A graphite discharge pipe provided so as to protrude from the center inside the graphitization furnace main body to the lower outside of the graphitization furnace main body,
A cutting hopper that is provided at the lower end of the graphite discharge pipe and cuts out the graphite flowing down the graphite discharge pipe and discharges it to the outside;
A turntable that is provided inside the cutting hopper and is disposed opposite to the lower end of the graphite discharge pipe and rotates horizontally;
A scraper provided inside the cut-out hopper, and dropping the graphite cut out on the turntable as the turntable rotates;
An integrated member that is provided inside the cutting hopper and receives the graphite dropped by the scraper;
A shielding valve for dropping and stopping the graphite accumulated continuously connected to the lower side of the collecting member;
A gas-air replacement hopper that is continuously provided below the shielding valve and temporarily stores graphite that is dropped through the shielding valve, and has an atmosphere similar to the outside air around the graphite.
A graphitization furnace comprising: a shielding valve that is provided below the gas / air replacement hopper and that discharges graphite from the gas / air replacement hopper to the outside .
黒鉛化炉本体と、該黒鉛化炉本体において生成された黒鉛を排出する黒鉛排出装置とを備えた黒鉛化炉であって、
前記黒鉛排出装置が、
前記黒鉛化炉本体の内部中央から当該黒鉛化炉本体の外部下方に突出して設けられた黒鉛排出管と、
該黒鉛排出管の下端部に設けられ、当該黒鉛排出管を流下する黒鉛を切り出して外部へ排出する切り出しホッパと、
該切り出しホッパの内部に設けられ、前記黒鉛排出管の下端に対向して配設されるとともに水平回転するターンテーブルと、
前記切り出しホッパの内部に設けられ、前記ターンテーブルの回転に伴い、当該ターンテーブル上に切り出された黒鉛を下方へ落下させるスクレーパと、
前記切り出しホッパの内部に設けられ、前記スクレーパによって落下させられた黒鉛を受け止める集積部材と、
該集積部材の下方に連設されて集積された黒鉛の落下およびその停止を行なう遮蔽弁と、
該遮蔽弁の下方に連設され、当該遮蔽弁を経て落下させられる黒鉛を一旦貯留するとともに、この黒鉛回りを外気と同様の雰囲気とするガス空気置換ホッパと、
該ガス空気置換ホッパの下方に連設され、当該ガス空気置換ホッパから黒鉛を外部に排出する遮蔽弁と
を備えることを特徴とする黒鉛化炉。
A graphitization furnace body, a graphitization furnace and a graphite discharge device for discharging the graphite produced in the graphitization furnace body,
The graphite discharge device
A graphite discharge pipe provided so as to protrude from the center inside the graphitization furnace main body to the lower outside of the graphitization furnace main body,
A cutting hopper that is provided at the lower end of the graphite discharge pipe and cuts out the graphite flowing down the graphite discharge pipe and discharges it to the outside;
A turntable that is provided inside the cutting hopper and is disposed opposite to the lower end of the graphite discharge pipe and rotates horizontally;
A scraper provided inside the cut-out hopper, and dropping the graphite cut out on the turntable as the turntable rotates;
An integrated member that is provided inside the cutting hopper and receives the graphite dropped by the scraper;
A shielding valve for dropping and stopping the graphite accumulated continuously connected to the lower side of the collecting member;
A gas-air replacement hopper that is provided below the shielding valve and temporarily stores graphite that is dropped through the shielding valve, and that makes the atmosphere around the graphite similar to the outside air,
A shielding valve connected to the lower side of the gas / air replacement hopper and discharging graphite from the gas / air replacement hopper to the outside;
Graphitization furnace, characterized in that it comprises a.
JP12251298A 1998-05-01 1998-05-01 Graphitization furnace Expired - Fee Related JP4096402B2 (en)

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KR102577347B1 (en) * 2023-06-06 2023-09-12 에스아이에스 주식회사 Multistage vertical graphitization furnace system
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JP2021105493A (en) * 2019-12-26 2021-07-26 日本電極株式会社 Heat treatment device for carbonaceous grain and method therefor
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KR102577347B1 (en) * 2023-06-06 2023-09-12 에스아이에스 주식회사 Multistage vertical graphitization furnace system
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