JPH06147778A - Tunnel kiln for baking carbon product - Google Patents
Tunnel kiln for baking carbon productInfo
- Publication number
- JPH06147778A JPH06147778A JP4328445A JP32844592A JPH06147778A JP H06147778 A JPH06147778 A JP H06147778A JP 4328445 A JP4328445 A JP 4328445A JP 32844592 A JP32844592 A JP 32844592A JP H06147778 A JPH06147778 A JP H06147778A
- Authority
- JP
- Japan
- Prior art keywords
- black smoke
- furnace
- furnace body
- temperature
- area
- 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
Links
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、熱分解により黒煙を発
生するタール、ピツチ等の結合剤を含有した炭素製品を
焼成するのに用いて好適なトンネルキルンに関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a tunnel kiln suitable for firing a carbon product containing a binder such as tar or pitch which produces black smoke by thermal decomposition.
【0002】[0002]
【従来の技術】トンネルキルンの一般構造を本発明の一
実施例を示す図1を参照して説明すると、トンネル状の
細長い炉体1内に予熱帯、焼成帯及び冷却帯が画成さ
れ、焼成帯でバーナ2から焚口3を通して燃焼ガスを噴
出する一方、予熱帯の入口側において煙道4から排気フ
アン5により炉内ガスを吸引して排気することによつ
て、炉体1内に同図に示すヒートカーブの温度雰囲気を
形成し、製品aを台車に載せて炉体1内を走行させる間
に、予熱、焼成及び冷却を順次に行うようになつてい
る。2. Description of the Related Art The general structure of a tunnel kiln will be described with reference to FIG. 1 showing an embodiment of the present invention. A pre-tropical zone, a firing zone and a cooling zone are defined in a tunnel-shaped elongated furnace body 1. While the combustion gas is ejected from the burner 2 through the combustion port 3 in the firing zone, while the in-furnace gas is sucked and exhausted from the flue 4 by the exhaust fan 5 on the inlet side of the pre-tropical zone, A temperature atmosphere of a heat curve shown in the figure is formed, and preheating, firing and cooling are sequentially performed while the product a is placed on a trolley and travels inside the furnace body 1.
【0003】そして、このようなトンネルキルンで、タ
ール、ピツチ等の結合剤を含有した炭素製品aを焼成す
る場合は、製品aが加熱されるに従つて結合剤が燃焼す
なわち熱分解することにより黒煙(ボラタイル)が発生
する。この黒煙は、製品aの温度が350℃位までは発
生が少なく、その温度を超えて800℃近くまでは激し
く発生し、それ以上になると自燃することが知られてい
る。When a carbon product a containing a binder such as tar or pitch is fired in such a tunnel kiln, the binder is burned, that is, thermally decomposed as the product a is heated. Black smoke (volatile) is generated. It is known that this black smoke is less generated up to a temperature of the product a of about 350 ° C., is violently generated up to about 800 ° C. above the temperature, and self-combusts when the temperature is higher than that.
【0004】[0004]
【発明が解決しようとする課題】従来のトンネルキルン
では、上記したように炉内ガスが低温部である予熱帯の
入口側に引かれて排気されるようになつているから、発
生した黒煙も燃焼することなくそのまま引かれて排出さ
れ、公害の原因となる。In the conventional tunnel kiln, as described above, since the in-furnace gas is drawn to the inlet side of the pre-tropical zone, which is the low temperature part, and exhausted, the black smoke generated is generated. Even if it is not burned, it is pulled and discharged as it is, causing pollution.
【0005】その防止対策として、排ガスをアフタバー
ナで加熱して黒煙を燃焼処理するこも行われているが、
そのためには、製品の焼成に使用するのにほぼ匹敵する
燃料が必要であつて、経費が嵩むという別の問題を抱え
ていた。As a preventive measure, exhaust gas is heated by an afterburner to burn black smoke.
This required nearly the same fuel to be used for firing the product, and had the additional problem of increased cost.
【0006】[0006]
【課題を解決するための手段】本発明の炭素製品焼成用
トンネルキルンは、叙上の点に鑑み完成されたものであ
つて、予熱帯の結合剤が熱分解して黒煙が発生する炉内
温度が350〜800℃の領域の炉内ガスを吸引して、
800℃以上の高温域の炉体内に打ち込む黒煙燃焼用手
段と、高温域の炉内ガスを吸引して、予熱帯の黒煙の発
生域よりも前の低温域に打ち込む熱量補充用手段とを設
けた構成とした。DISCLOSURE OF THE INVENTION The tunnel kiln for burning carbon products of the present invention has been completed in view of the above points, and is a furnace in which a binder in the pretropical zone is thermally decomposed to generate black smoke. By sucking in the furnace gas in the region where the internal temperature is 350 to 800 ° C,
A means for burning black smoke to be injected into the furnace body in the high temperature range of 800 ° C or higher, and a means for supplementing the amount of heat to suck in the gas in the furnace in the high temperature area and drive it into the low temperature area before the black smoke generation area in the pre-tropical zone. Is provided.
【0007】[0007]
【作用】予熱帯の炉内温度が350〜800℃の領域で
結合剤が熱分解することにより黒煙が発生するが、その
黒煙を含んだ炉内ガスは黒煙燃焼用手段によつて吸引さ
れて800℃以上の高温域に打ち込まれ、そこにおいて
黒煙が燃焼されて消失する。[Function] Black smoke is generated by the thermal decomposition of the binder in the pre-tropical furnace temperature range of 350 to 800 ° C. The furnace gas containing the black smoke is discharged by the means for burning black smoke. It is sucked and driven into a high temperature range of 800 ° C or higher, where black smoke burns and disappears.
【0008】上記の黒煙発生域で炉内ガスが吸引される
ことによつて、予熱帯のそれより前の低温部で熱量が不
足することとなるが、熱量補充用手段によつて高温部か
ら吸引した炉内ガスが低温部に打ち込まれ、不足熱量が
補充される。Since the gas in the furnace is sucked in the above-mentioned black smoke generation area, the heat quantity becomes insufficient in the low temperature part before the pre-tropical zone, but the high temperature part is obtained by the heat quantity supplementing means. The in-furnace gas sucked from is driven into the low temperature part to replenish the insufficient heat amount.
【0009】[0009]
【実施例】以下、本発明の一実施例を図1に基づいて説
明する。本実施例では、既述した構造のトンネルキルン
において、予熱帯の炉内温度が350〜800℃近くの
領域の側壁に、吸引フアン12に接続された炉内ガス吸
引口11が形成され、その吸引フアン12の打ち込み先
が、バーナ2の燃焼空気供給口2aに接続されている。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to FIG. In this embodiment, in the tunnel kiln having the structure described above, the in-furnace gas suction port 11 connected to the suction fan 12 is formed on the side wall of the region where the pre-tropical in-furnace temperature is near 350 to 800 ° C. The driving destination of the suction fan 12 is connected to the combustion air supply port 2a of the burner 2.
【0010】また、予熱帯の炉内温度が800℃以上と
なる高温部の側壁には、打込フアン14に接続された熱
風吸引口13が形成され、その打込フアン14の打ち込
み先が、予熱帯の炉内温度が350℃以下となる入口側
の側壁に形成された熱風打込口15に接続されている。Further, a hot air suction port 13 connected to a driving fan 14 is formed on the side wall of a high temperature part where the temperature in the pre-tropical furnace is 800 ° C. or more, and the driving fan 14 is driven into a hot air suction port 13. It is connected to the hot air blowing port 15 formed on the side wall on the inlet side where the temperature in the pre-tropical furnace becomes 350 ° C. or lower.
【0011】本実施例はこのような構造になり、予熱帯
の炉内温度が350〜800℃の領域で炭素製品a中に
含まれた結合剤が熱分解することにより黒煙が発生する
が、その黒煙を含んだ炉内ガスは炉内ガス吸引口11か
ら吸引フアン12により吸引されて、バーナ2の燃焼空
気の一部として打ち込まれ、それによつて黒煙が燃焼さ
れて消失する。This embodiment has such a structure, and black smoke is generated due to the thermal decomposition of the binder contained in the carbon product a in the temperature range of 350 to 800 ° C. in the pretropical furnace. The in-furnace gas containing the black smoke is sucked from the in-furnace gas suction port 11 by the suction fan 12 and is injected as a part of the combustion air of the burner 2, whereby the black smoke is burned and disappears.
【0012】また、上記の黒煙発生域で炉内ガスが吸引
されることによつて、予熱帯のそれより前の低温部では
熱量が不足することとなるが、予熱帯の800℃以上の
高温部において黒煙が自燃することにより黒煙を含んで
いない状態の炉内ガスが、熱風吸引口13から打込フア
ン14によつて吸引されて、予熱帯の入口側の低温部に
熱風打込口15から打ち込まれる。それにより、予熱帯
の低温部の不足熱量が補充されて、所定のヒートカーブ
が維持される。Further, since the in-furnace gas is sucked in the above black smoke generation region, the heat quantity becomes insufficient in the low temperature portion before the pre-tropical zone, but it is higher than 800 degrees Celsius in the pre-tropical zone. The in-furnace gas containing no black smoke due to self-combustion of black smoke in the high temperature part is sucked by the driving fan 14 from the hot air suction port 13 and blown into the low temperature part on the inlet side of the pre-tropical zone with hot air. It is driven in through the insertion port 15. As a result, the insufficient heat quantity in the low temperature part of the pre-tropical zone is replenished, and the predetermined heat curve is maintained.
【0013】なお、黒煙を含んだ炉内ガスの打ち込み先
は、焼成帯の焚口3や、焼成帯の炉体1内、さらには、
予熱帯の炉内温度が800℃以上となる領域であつても
よい。[0013] The furnace gas containing black smoke is injected into the firing port 3 of the firing zone, the furnace body 1 of the firing zone, and
It may be a region where the temperature in the pre-tropical furnace is 800 ° C or higher.
【0014】[0014]
【発明の効果】以上説明したとおり、本発明によれば、
発生した黒煙が高温部で燃焼されることにより炉体内で
消失処理されて、外部に排出されるのが防止され、しか
も、焼成用燃料のみで黒煙の燃焼処理ができるから、経
費増を招くおそれもない。As described above, according to the present invention,
The generated black smoke is burnt in the high temperature part and is eliminated in the furnace body to be prevented from being discharged to the outside. Moreover, the burning process of the black smoke can be performed only by the burning fuel, which increases the cost. There is no fear of inviting.
【0015】また、予熱帯の黒煙発生域よりも前を領域
での不足熱量も補充されて、所定のヒートカーブを維持
できる効果がある。In addition, an insufficient amount of heat in the area before the black smoke generation area in the pre-tropical zone is replenished, and a predetermined heat curve can be maintained.
【図1】本発明の一実施例の構成図並びにヒートカーブ
のグラフである。FIG. 1 is a configuration diagram and a heat curve graph of an embodiment of the present invention.
a:炭素製品 1:炉体 2a:(バーナ2の)燃焼空
気供給口 11:炉内ガス吸引口 12:吸引フアン
13:熱風吸引口 14:打込フアン 15:熱風打込
口a: carbon product 1: furnace body 2a: combustion air supply port (for burner 2) 11: furnace gas suction port 12: suction fan
13: Hot air inlet 14: Driving fan 15: Hot air inlet
Claims (1)
た炭素製品を台車上に載せてトンネル状の炉体内を走行
させる間に、該炉体内に形成された一定のヒートカーブ
の温度雰囲気に従つて予熱、焼成及び冷却を順次に行う
ようにした炭素製品焼成用トンネルキルンにおいて、 予熱帯の前記結合剤が熱分解して黒煙が発生する炉内温
度が350〜800℃の領域の炉内ガスを吸引して、8
00℃以上の高温域の炉体内に打ち込む黒煙燃焼用手段
と、前記高温域の炉内ガスを吸引して、予熱帯の前記黒
煙の発生域よりも前の低温域に打ち込む熱量補充用手段
とを設けたことを特徴とする炭素製品焼成用トンネルキ
ルン。1. While a carbon product containing tar, pitch, etc. as a binder is placed on a trolley and travels in a tunnel-shaped furnace body, the temperature atmosphere of a constant heat curve formed in the furnace body is followed. In a tunnel kiln for firing carbon products, which is preheated, fired, and cooled in sequence, the binder in the preheat zone is thermally decomposed to generate black smoke. The furnace temperature is in the range of 350 to 800 ° C. Inhale gas, 8
Means for burning black smoke to be injected into the furnace body in a high temperature range of 00 ° C or higher, and for supplementing the amount of heat to be sucked into the furnace gas in the high temperature area and to be injected into the low temperature area before the black smoke generation area in the pretropical zone A tunnel kiln for firing carbon products, characterized by being provided with means.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32844592A JP3263906B2 (en) | 1992-11-12 | 1992-11-12 | Tunnel kiln for firing carbon products |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32844592A JP3263906B2 (en) | 1992-11-12 | 1992-11-12 | Tunnel kiln for firing carbon products |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH06147778A true JPH06147778A (en) | 1994-05-27 |
JP3263906B2 JP3263906B2 (en) | 2002-03-11 |
Family
ID=18210358
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP32844592A Expired - Lifetime JP3263906B2 (en) | 1992-11-12 | 1992-11-12 | Tunnel kiln for firing carbon products |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3263906B2 (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001527202A (en) * | 1997-12-22 | 2001-12-25 | コーニング インコーポレイテッド | Method for firing ceramic honeycomb body and tunnel kiln used for firing |
CN102478350A (en) * | 2010-11-22 | 2012-05-30 | 福建泉州顺美集团有限责任公司 | Dual-return-air high-efficiency and energy-saving tunnel kiln |
CN104713356A (en) * | 2013-12-12 | 2015-06-17 | 福建中茂精密铸造有限公司 | Novel calcining kiln |
CN104713359A (en) * | 2015-03-16 | 2015-06-17 | 霍山县永科新能源有限公司 | Solid bamboo charcoal processing furnace kiln system |
CN105241261A (en) * | 2015-11-02 | 2016-01-13 | 承德联玉体育文化发展有限公司 | Waste heat recovery device for tunnel kiln |
CN115790226A (en) * | 2022-11-21 | 2023-03-14 | 乌兰察布市旭峰炭素科技有限公司 | Heat transfer oil heat exchange system for carbon production |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102829624B (en) * | 2012-09-20 | 2014-05-21 | 惠州市方诚实业有限公司 | Desulfuration and impurity removal device and process of tunnel kiln exhaust gas |
-
1992
- 1992-11-12 JP JP32844592A patent/JP3263906B2/en not_active Expired - Lifetime
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001527202A (en) * | 1997-12-22 | 2001-12-25 | コーニング インコーポレイテッド | Method for firing ceramic honeycomb body and tunnel kiln used for firing |
JP2008285407A (en) * | 1997-12-22 | 2008-11-27 | Corning Inc | Method for firing ceramic honeycomb body |
JP4723085B2 (en) * | 1997-12-22 | 2011-07-13 | コーニング インコーポレイテッド | Method for firing ceramic honeycomb body and tunnel kiln used for firing |
CN102478350A (en) * | 2010-11-22 | 2012-05-30 | 福建泉州顺美集团有限责任公司 | Dual-return-air high-efficiency and energy-saving tunnel kiln |
CN104713356A (en) * | 2013-12-12 | 2015-06-17 | 福建中茂精密铸造有限公司 | Novel calcining kiln |
CN104713359A (en) * | 2015-03-16 | 2015-06-17 | 霍山县永科新能源有限公司 | Solid bamboo charcoal processing furnace kiln system |
CN105241261A (en) * | 2015-11-02 | 2016-01-13 | 承德联玉体育文化发展有限公司 | Waste heat recovery device for tunnel kiln |
CN115790226A (en) * | 2022-11-21 | 2023-03-14 | 乌兰察布市旭峰炭素科技有限公司 | Heat transfer oil heat exchange system for carbon production |
CN115790226B (en) * | 2022-11-21 | 2023-12-26 | 乌兰察布市旭峰炭素科技有限公司 | Heat transfer oil heat exchange system for carbon production |
Also Published As
Publication number | Publication date |
---|---|
JP3263906B2 (en) | 2002-03-11 |
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