JP2000356476A - Facilities for treatment of exhaust gas of electric furnace - Google Patents

Facilities for treatment of exhaust gas of electric furnace

Info

Publication number
JP2000356476A
JP2000356476A JP11165310A JP16531099A JP2000356476A JP 2000356476 A JP2000356476 A JP 2000356476A JP 11165310 A JP11165310 A JP 11165310A JP 16531099 A JP16531099 A JP 16531099A JP 2000356476 A JP2000356476 A JP 2000356476A
Authority
JP
Japan
Prior art keywords
exhaust gas
dust
electric furnace
equipment
dust removing
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.)
Withdrawn
Application number
JP11165310A
Other languages
Japanese (ja)
Inventor
Makoto Takahashi
誠 高橋
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel 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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP11165310A priority Critical patent/JP2000356476A/en
Publication of JP2000356476A publication Critical patent/JP2000356476A/en
Withdrawn legal-status Critical Current

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  • Incineration Of Waste (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
  • Furnace Details (AREA)

Abstract

PROBLEM TO BE SOLVED: To prevent regeneration of harmful components due to soot and dust in exhaust gas, in facilities for treatment of exhaust gas which disposes of the exhaust gas produced from an electric furnace. SOLUTION: Exhaust gas produced from an electric furnace or a scrap preheating apparatus for the electric furnace is introduced into a combustion apparatus 2 through a duct and combusted therein. Cooling equipment 4 which cools down the exhaust gas combusted in the combustion apparatus 2 to a prescribed temperature is connected to the downstream side of the apparatus and the gas cooled down is then subjected to dust collection by a filter type dust collector 5. In facilities for disposal of exhaust gas having this constitution, dust removing equipment 3 collecting soot and dust in the exhaust gas is provided between the combustion apparatus 2 and the cooling equipment 4. This dust removing equipment 3, as dust removing equipment of a cyclone type or an inertial impaction type, removes the soot and dust in the exhaust gas beforehand.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、電気炉から発生す
る排ガスを処理する排ガス処理設備に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an exhaust gas treatment facility for treating exhaust gas generated from an electric furnace.

【0002】[0002]

【従来の技術】金属材料を電気炉またはスクラップ予熱
装置にて予熱する場合、予熱の際に発生した排ガス中に
有害成分として白煙・悪臭・芳香族塩素化合物等が発生
し、作業環境上あるいは、環境上問題となっている。
2. Description of the Related Art When preheating metal materials in an electric furnace or a scrap preheating device, white smoke, odors, aromatic chlorine compounds, etc. are generated as harmful components in exhaust gas generated at the time of preheating. , Is an environmental problem.

【0003】有害成分は有機塩素系の物質が化学反応す
る過程で発生する。電気炉においては、電気炉から発生
する排ガスを完全燃焼させるため、燃焼塔が設置されて
いるが、電気炉からの発生する排ガス発生量あるいは排
ガス成分の変動により、不完全燃焼が起こりやすく、有
害成分も発生しやすいと言われている。また、完全燃焼
しても排ガス中に分解された塩素・炭素・水素等が漂っ
ており、排ガスが300℃前後に冷却された段階で、排
ガス中の煤塵が触媒となって有害成分が再生成されると
いわれている。
[0003] Harmful components are generated in the course of chemical reaction of organic chlorine-based substances. In the electric furnace, a combustion tower is installed to completely combust the exhaust gas generated from the electric furnace.However, incomplete combustion is likely to occur due to fluctuations in the amount of exhaust gas generated from the electric furnace or exhaust gas components, and harmful It is said that components are also likely to occur. Also, even after complete combustion, decomposed chlorine, carbon, hydrogen, etc. are drifting in the exhaust gas, and when the exhaust gas is cooled down to around 300 ° C, dust in the exhaust gas becomes a catalyst to regenerate harmful components. It is said to be done.

【0004】例えば特開平9−133476号公報に記
載の発明では、電気炉用予熱装置から排出された排ガス
を処理する燃焼塔に2基1組の蓄熱式熱交換器を設け
て、スクラップ予熱装置から排出された排ガスが、一方
側の蓄熱式熱交換器を通過して燃焼塔に送られ、空気吹
き込み器から空気を供給して燃焼塔内で800℃以上に
燃焼させ、他方側の蓄熱式熱交換器を通ってこの排ガス
を150℃以下に冷却し排出ダクトに導き、バグフィル
ターを通って大気に放出する。このときスクラップ予熱
装置と蓄熱交換器の間には、ダクトコレクターが配置さ
れ、燃焼塔で燃焼した排ガスを排出する際に発生するダ
スト中、大きいダストを捕集するようにしている。ま
た、特開平6−117780号公報に電気炉または電気
炉用スクラップ予熱装置からの排ガスを燃焼塔内バーナ
ーで燃焼加熱することにより有害成分を分解後、ガスク
ーラにて急冷することにより有害成分の再合成を防ぎ、
さらに後流にバグフィルターを設けることにより、排ガ
ス中に含まれる有害成分を除去する方法が開示されてい
る。
[0004] For example, in the invention described in Japanese Patent Application Laid-Open No. 9-133476, a pair of regenerative heat exchangers are provided in a combustion tower for treating exhaust gas discharged from a preheating device for an electric furnace, and a scrap preheating device is provided. Exhaust gas discharged from is passed through the regenerative heat exchanger on one side and sent to the combustion tower, and air is supplied from an air blower to burn in the combustion tower at 800 ° C or higher, and the regenerative heat on the other side The exhaust gas is cooled to 150 ° C. or lower through a heat exchanger, guided to a discharge duct, and discharged to the atmosphere through a bag filter. At this time, a duct collector is arranged between the scrap preheating device and the heat storage exchanger to collect large dust in dust generated when exhaust gas discharged from the combustion tower is discharged. Japanese Patent Application Laid-Open No. HEI 6-117780 discloses that after decomposing harmful components by burning exhaust gas from an electric furnace or a scrap preheating device for an electric furnace using a burner in a combustion tower, the harmful components are decomposed and then rapidly cooled by a gas cooler. Prevent synthesis,
Further, there is disclosed a method of removing harmful components contained in exhaust gas by providing a bag filter in a downstream side.

【0005】上記特開平9−133476号公報に記載
された発明は、燃焼塔に蓄熱式熱交換器を配置して、蓄
熱式熱交換器を交互に切り替えて煤塵を含む排ガスを8
00℃以上で加熱燃焼して排ガス中の有害成分は大部分
が熱分解され、その後急速に冷却して再合成を妨げ、低
レベルで維持する。その後排ガスは濾過式集塵設備に導
入され、濾過式集塵設備によりさらに有害成分を除去し
ようとするものである。
The invention described in Japanese Patent Application Laid-Open No. Hei 9-133476 discloses a method in which a regenerative heat exchanger is arranged in a combustion tower, and the regenerative heat exchangers are alternately switched to discharge exhaust gas containing dust.
Most of the harmful components in the exhaust gas are thermally decomposed by heating and burning at a temperature of 00 ° C. or higher, and then cooled rapidly to prevent resynthesis and maintain a low level. Thereafter, the exhaust gas is introduced into a filtration type dust collecting facility, and further attempts to remove harmful components by the filtering type dust collecting facility.

【0006】また、特開平6−117780号公報記載
の発明は、電気炉または電気炉用スクラップ予熱装置か
らの排ガスを燃焼塔内バーナーで燃焼加熱し、加熱した
排ガスをある一定時間以上保持室内で保持し、有害成分
を分解させ、かつ、保持室の出側に連接したスプレーク
ーラーにより直接排ガスを冷却し、有害成分の再生成を
防止しようとするものである。
The invention described in Japanese Patent Application Laid-Open No. HEI 6-117780 discloses a method in which exhaust gas from an electric furnace or a scrap preheating device for an electric furnace is burned and heated by a burner in a combustion tower, and the heated exhaust gas is kept in a holding chamber for a certain period of time or more. The purpose is to hold and decompose harmful components, and to directly cool the exhaust gas by a spray cooler connected to the outlet side of the holding chamber to prevent the regeneration of harmful components.

【0007】[0007]

【発明が解決しようとする課題】しかし、金属材料を電
気炉またはスクラップ予熱装置にて予熱する際に発生す
る排ガス量は80tクラスの電気炉で約2000Nm3
/minで、排ガス中には約8g/Nm3の煤塵が含ま
れている。この煤塵を含む排ガスを燃焼塔または、燃焼
混合装置で燃焼加熱しても、排ガス中の有害成分は熱分
解されるが、排ガス中のダストは温度が上昇するだけで
そのまま蓄熱式熱交換器及びダストコレクターまたは冷
却設備に導入され、冷却された排ガスはフィルターでダ
ストを回収されて大気へ放散される。特開平9−133
476号公報に記載の方法では、スクラップ予熱装置で
発生する煤塵を含む排ガスを蓄熱式熱交換器に導入する
と、熱交換器内の蓄熱部に使用する蓄熱材に煤塵が付着
し、蓄熱部に煤塵の目詰まりが発生し、熱交換が不可能
となる。
However, the amount of exhaust gas generated when a metal material is preheated by an electric furnace or a scrap preheating device is about 2000 Nm 3 in an 80 t class electric furnace.
/ Min, about 8 g / Nm 3 in the exhaust gas. The harmful components in the exhaust gas are thermally decomposed even if the exhaust gas containing the dust is heated by combustion in a combustion tower or a combustion mixing device, but the dust in the exhaust gas only increases in temperature, and the heat storage type heat exchanger and The exhaust gas that has been introduced into a dust collector or cooling facility and cooled is collected by a filter to collect dust and is released to the atmosphere. JP-A-9-133
According to the method described in Japanese Patent No. 476, when exhaust gas containing dust generated in the scrap preheating device is introduced into the regenerative heat exchanger, the dust adheres to the heat storage material used for the heat storage unit in the heat exchanger, and Dust clogging occurs and heat exchange becomes impossible.

【0008】また、特開平6−117780号公報で
は、煤塵を含む排ガスを燃焼混合装置で熱分解し、そし
て保持室で一定時間保持した有害成分の再生成を防止、
そして、出側の冷却設備にて急激に冷却している。この
装置では、冷却設備としてスプレークーラを使用してい
るため、煤塵を含む排ガスが冷却設備のスプレー水で冷
却されると排ガス中の煤塵も洗い流され、煤塵は、流動
状のダストとなり、後段でのダスト処理に大がかりな設
備が必要となる。
In Japanese Patent Application Laid-Open No. Hei 6-117780, exhaust gas containing dust is thermally decomposed by a combustion and mixing device, and harmful components held in a holding chamber for a certain period of time are prevented from being regenerated.
And it is rapidly cooled by the cooling equipment on the outlet side. In this device, a spray cooler is used as cooling equipment, so when the exhaust gas containing dust is cooled by the spray water of the cooling equipment, the dust in the exhaust gas is also washed away, and the dust becomes fluid dust, and in the subsequent stage, Large-scale equipment is required for the treatment of dust.

【0009】[0009]

【課題を解決するための手段】電気炉または電気炉用ス
クラップ予熱装置から発生する排ガスをダクトを介して
燃焼塔に導入して前記排ガスを燃焼させ、その後流に前
記燃焼塔で燃焼した排ガスを所定の温度冷却する冷却設
備を連結してその後濾過式集塵設備で集塵する排ガス処
理設備において、前記燃焼塔と冷却設備の間に排ガス中
の煤塵を捕集する除塵設備を配設したことおよび前記除
塵設備は、サイクロン式除塵設備または衝突型除塵設備
として排ガス中の煤塵を事前に除去するものである。
An exhaust gas generated from an electric furnace or a scrap preheating device for an electric furnace is introduced into a combustion tower through a duct to burn the exhaust gas, and the exhaust gas burned by the combustion tower is supplied to a subsequent stream. In an exhaust gas treatment facility that connects a cooling facility that cools to a predetermined temperature and then collects dust with a filtration type dust collection facility, a dust removal facility that collects dust in exhaust gas is disposed between the combustion tower and the cooling facility. In addition, the dust removing equipment removes dust in exhaust gas in advance as a cyclone dust removing equipment or a collision type dust removing equipment.

【0010】[0010]

【発明の実施の形態】図1は本発明の設備構成図であ
る。
DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is a diagram showing the equipment configuration of the present invention.

【0011】図1において、電気炉1に投入された金属
材料及びスクラップは予熱、溶解される。このとき発生
する排ガスは電気炉に連結したダクト9を介して燃焼塔
2に流入する。燃焼塔は、電気炉から発生した排ガス中
の未燃ガスを完全燃焼させながら排ガス中の有害成分を
分解させる装置で、燃焼の結果排ガス温度は800℃以
上になる。そして燃焼塔で完全燃焼した排ガスの温度
が、有害成分が再生成する温度である300〜500℃
まで低下する前に除塵設備3へと流入するように除塵設
備3を配置する。除塵設備3では、排ガス中に含まれる
煤塵を除去し、除去した排ガスを出側に配置した冷却設
備4に導入し、所定の温度に冷却してその後段に配置し
た集塵設備5へと導き、有害成分を捕獲し、煙突6を介
して大気へ放散する。
In FIG. 1, the metal material and scrap put into the electric furnace 1 are preheated and melted. The exhaust gas generated at this time flows into the combustion tower 2 via the duct 9 connected to the electric furnace. The combustion tower is a device for decomposing harmful components in exhaust gas while completely burning unburned gas in the exhaust gas generated from the electric furnace. As a result of the combustion, the temperature of the exhaust gas becomes 800 ° C. or higher. The temperature of the exhaust gas completely burned in the combustion tower is 300 to 500 ° C., which is the temperature at which the harmful components are regenerated.
The dust removing equipment 3 is arranged so as to flow into the dust removing equipment 3 before the dust removing equipment 3 is lowered. In the dust removal equipment 3, dust contained in the exhaust gas is removed, the removed exhaust gas is introduced into the cooling equipment 4 arranged on the outlet side, cooled to a predetermined temperature, and guided to the dust collection equipment 5 arranged in the subsequent stage. , Captures harmful components and emits them through the chimney 6 to the atmosphere.

【0012】80tクラスの電気炉では、排ガス量とし
て、約2000Nm3/minの排ガスが発生する。こ
の排ガス中には、約8g/Nm3の煤塵が含まれてい
る。即ち、2000Nm3/minの排ガス中には16
Kg/minの煤塵が含まれている。
In an electric furnace of the 80t class, an exhaust gas amount of about 2000 Nm 3 / min is generated. This exhaust gas contains about 8 g / Nm 3 of dust. That is, in the exhaust gas of 2000 Nm 3 / min, 16
Kg / min dust is contained.

【0013】燃焼塔2と冷却設備4との間に除塵設備3
を有しない場合には、燃焼塔2で排ガス中の有害成分を
熱分解しても、排ガスがダクトを介して冷却設備4へ導
入されるまでには、排ガス温度が低下して、排ガス中に
含まれる煤塵が触媒作用をつとめ、有害成分が再生成し
てしまう。本発明においては、燃焼塔2と冷却設備4と
の間に除塵設備3を有しているため、触媒作用をする煤
塵を有害成分が再生成するまでに煤塵の大半を除去する
ことができ、有害成分再生成の比率を低減することがで
きる。
A dust removing device 3 is provided between the combustion tower 2 and the cooling device 4.
In the case where no exhaust gas is contained, even if the harmful components in the exhaust gas are thermally decomposed in the combustion tower 2, the exhaust gas temperature decreases until the exhaust gas is introduced into the cooling facility 4 through the duct, and the exhaust gas contains The contained dust acts as a catalyst and harmful components are regenerated. In the present invention, since the dust removing device 3 is provided between the combustion tower 2 and the cooling device 4, most of the dust can be removed before the harmful component regenerates the dust acting as a catalyst, The rate of harmful component regeneration can be reduced.

【0014】除塵設備3として、サイクロン型除塵設備
や衝突型除塵設備を使用する。除塵設備の効率は高い方
がよいが、排ガス中の煤塵が少しでも減少できれば、二
次側で発生する有害成分の再生成は減少できる。また、
排ガス中の煤塵が減少すれば、熱分解後の有害成分が煤
塵に接触することも減少でき、有害成分の再生成は減少
するので、有害成分が所定の許容値であれば、冷却温度
を上げることができ、冷却設備の設備費を低減すること
ができる。また、冷却後の排ガス温度を一定とすれば、
有害成分の放出量を低下する事ができる。除塵設備3が
除塵した煤塵は搬送装置を介してホッパー8に回収す
る。
As the dust removing equipment 3, a cyclone dust removing equipment or a collision type dust removing equipment is used. The higher the efficiency of the dust removal equipment, the better, but if the dust in the exhaust gas can be reduced even a little, the regeneration of harmful components generated on the secondary side can be reduced. Also,
If the dust in the exhaust gas is reduced, it is possible to reduce the contact of the harmful component after thermal decomposition with the dust, and the regeneration of the harmful component is reduced. Therefore, if the harmful component has a predetermined allowable value, the cooling temperature is increased. And the equipment cost of the cooling equipment can be reduced. If the temperature of the exhaust gas after cooling is constant,
The release amount of harmful components can be reduced. The dust removed by the dust removing equipment 3 is collected in the hopper 8 via the transport device.

【0015】[0015]

【発明の効果】このように、排ガス中に含まれる煤塵が
触媒作用をする前に除去することで、有害成分の再生成
が防止でき、冷却設備で所定の温度に冷却する場合は、
有害成分の放出量を減少出来、また、有害成分の許容値
を一定にすれば、冷却温度を上げることができるので冷
却設備の設備費が大幅に削減する事ができる。このよう
に本発明の設備的効果は非常に大きく、操業コスト効果
にも大きく貢献する。
As described above, by removing the dust contained in the exhaust gas before catalyzing it, it is possible to prevent harmful components from being regenerated, and when cooling to a predetermined temperature with cooling equipment,
If the release amount of the harmful component can be reduced and the allowable value of the harmful component is kept constant, the cooling temperature can be raised, so that the equipment cost of the cooling equipment can be greatly reduced. As described above, the facility effect of the present invention is very large, and greatly contributes to the operation cost effect.

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

【図1】本発明を示す設備構成図。FIG. 1 is a configuration diagram of the equipment showing the present invention.

【符号の説明】[Explanation of symbols]

1 電気炉 2 燃焼塔 3 除塵設備 4 冷却設備 5 集塵設備 6 煙突 7 搬送装置 8 ホッパー 9 ダクト DESCRIPTION OF SYMBOLS 1 Electric furnace 2 Combustion tower 3 Dust removal equipment 4 Cooling equipment 5 Dust collection equipment 6 Chimney 7 Transport device 8 Hopper 9 Duct

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 電気炉または電気炉用スクラップ予熱装
置から発生する排ガスをダクトを介して燃焼塔に導入し
て前記排ガスを燃焼させ、その後流に前記燃焼塔で燃焼
した排ガスを冷却する冷却設備を連結してその後濾過式
集塵設備で集塵する排ガス処理設備において、 前記燃焼塔と冷却設備の間に排ガス中の煤塵を捕集する
除塵設備を配設したことを特徴とする電気炉の排ガス処
理設備。
1. A cooling system for introducing exhaust gas generated from an electric furnace or a scrap preheating device for an electric furnace into a combustion tower via a duct to burn the exhaust gas, and cooling the exhaust gas burned in the combustion tower in a subsequent stream. In an exhaust gas treatment facility that collects dust with a filtration type dust collection facility after coupling, a dust removal facility that collects dust in exhaust gas is disposed between the combustion tower and the cooling facility. Exhaust gas treatment equipment.
【請求項2】 前記除塵設備は、サイクロン式除塵設備
または衝突型除塵設備としたことを特徴とする請求項1
の電気炉の排ガス処理設備。
2. The dust removing equipment according to claim 1, wherein the dust removing equipment is a cyclone type dust removing equipment or a collision type dust removing equipment.
Exhaust gas treatment equipment for electric furnaces.
JP11165310A 1999-06-11 1999-06-11 Facilities for treatment of exhaust gas of electric furnace Withdrawn JP2000356476A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11165310A JP2000356476A (en) 1999-06-11 1999-06-11 Facilities for treatment of exhaust gas of electric furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11165310A JP2000356476A (en) 1999-06-11 1999-06-11 Facilities for treatment of exhaust gas of electric furnace

Publications (1)

Publication Number Publication Date
JP2000356476A true JP2000356476A (en) 2000-12-26

Family

ID=15809912

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11165310A Withdrawn JP2000356476A (en) 1999-06-11 1999-06-11 Facilities for treatment of exhaust gas of electric furnace

Country Status (1)

Country Link
JP (1) JP2000356476A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009228974A (en) * 2008-03-24 2009-10-08 Furukawa Electric Co Ltd:The Exhaust gas treating facility and exhaust gas treating method
CN102445085A (en) * 2010-10-08 2012-05-09 王全祥 High-temperature flue gas and dust dry purification and waste heat recovery process for ore furnace
JP2021105470A (en) * 2019-12-26 2021-07-26 中外炉工業株式会社 Exhaust gas treatment device for electric furnace

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009228974A (en) * 2008-03-24 2009-10-08 Furukawa Electric Co Ltd:The Exhaust gas treating facility and exhaust gas treating method
CN102445085A (en) * 2010-10-08 2012-05-09 王全祥 High-temperature flue gas and dust dry purification and waste heat recovery process for ore furnace
JP2021105470A (en) * 2019-12-26 2021-07-26 中外炉工業株式会社 Exhaust gas treatment device for electric furnace
JP7102084B2 (en) 2019-12-26 2022-07-19 中外炉工業株式会社 Electric furnace exhaust gas treatment equipment

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