JPH07146082A - Exhaust gas treating method for electric furnace - Google Patents

Exhaust gas treating method for electric furnace

Info

Publication number
JPH07146082A
JPH07146082A JP5292226A JP29222693A JPH07146082A JP H07146082 A JPH07146082 A JP H07146082A JP 5292226 A JP5292226 A JP 5292226A JP 29222693 A JP29222693 A JP 29222693A JP H07146082 A JPH07146082 A JP H07146082A
Authority
JP
Japan
Prior art keywords
exhaust gas
scrap
electric furnace
chlorine
passed
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.)
Pending
Application number
JP5292226A
Other languages
Japanese (ja)
Inventor
Seiji Yamada
山田  清二
Takekazu Suzuki
武和 鈴木
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.)
Topy Industries Ltd
Original Assignee
Topy Industries Ltd
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 Topy Industries Ltd filed Critical Topy Industries Ltd
Priority to JP5292226A priority Critical patent/JPH07146082A/en
Publication of JPH07146082A publication Critical patent/JPH07146082A/en
Pending legal-status Critical Current

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

Abstract

PURPOSE:To fix chlorine, etc., generated at the time of preheating as chloride and to reduce generation of organic chlorine compound itself by adding salt of at least one type of element selected from alkalis to scrap when the scrap is preheated by exhaust gas of an electric furnace. CONSTITUTION:Exhaust gas from an electric furnace 1 is guided to a burnings tower 2 to burn unburnt components. In this case, since the gas has a high temperature and large energy, it is partly passed through a plurality of scrap preheaters 3 to preheat shredder scraps of a waste vehicle. The gas is sucked to a main blower 7, guided to a plurality of spraying towers 8 and cooled. Then, the gas is passed through a bag dust collector 9 to remove dusts and condensed organic components. In this case, salt of at least one element selected from alkalis and alkaline earth elements is added in the preheater 3. Thus, chlorine, etc., generated when vinyl chloride in the scrap is thermally decomposed is fixed as chloride.

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、電気炉排ガス処理方法
に関し、とくに排ガスでスクラップを予熱するときに生
じる有機塩素化合物の系外への排出を低減させることが
できる排ガス処理方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electric furnace exhaust gas treatment method, and more particularly to an exhaust gas treatment method capable of reducing the emission of organochlorine compounds out of the system when preheating scrap with exhaust gas.

【0002】[0002]

【従来の技術】製鋼用原料を電気炉に投入して溶解、精
錬する際に電気炉から発生する排ガスは、燃焼塔に通さ
れて未然有機化合物等を完全燃焼され無害化がはかられ
た後に冷却、集塵等の処理が施され、系外に排出され
る。しかし、電気炉の高温排ガスのもつ熱エネルギーを
一部回収するために、燃焼塔を通した後の排ガスをスク
ラップ予熱装置に通す場合には、スクラップに含まれて
いる塩化ビニルや極圧添加剤を含む加工油等が排ガスに
接触して、未完全燃焼の有機塩素化合物を生成するおそ
れがあり、そのような有機化合物は発生しても捕集され
るべきである。従来のスクラップ予熱装置をもつ電気炉
では、スクラップ予熱装置を通った後の排ガスの温度を
できるだけ下げ、バグフィルタでダストと共に捕捉する
方法がとられている。
2. Description of the Related Art Exhaust gas generated from an electric furnace when a steelmaking raw material is charged into the electric furnace to be melted and refined is passed through a combustion tower to completely burn organic compounds and detoxify them. After that, it is cooled, dust-collected, etc., and discharged to the outside of the system. However, in order to partially recover the thermal energy of the high-temperature exhaust gas of the electric furnace, when the exhaust gas after passing through the combustion tower is passed through the scrap preheater, the vinyl chloride and extreme pressure additives contained in the scrap are There is a risk that processing oils and the like containing will come into contact with the exhaust gas and produce incompletely combusted organic chlorine compounds, and such organic compounds should be collected even if they occur. In a conventional electric furnace having a scrap preheating device, a method is adopted in which the temperature of the exhaust gas after passing through the scrap preheating device is lowered as much as possible, and is captured together with dust by a bag filter.

【0003】[0003]

【発明が解決しようとする課題】従来は、スクラップ予
熱装置内での有機塩素化合物の発生を容認し、発生後の
捕捉効率の向上で対処していたと云える。しかし、原料
スクラップ中に塩化ビニルを含むダストおよび極圧添加
剤を含む加工油が大量に存在した場合には、スクラップ
予熱装置内での有機塩素化合物の発生もそれだけ多くな
り、捕捉効率の向上だけでは対処しきれなくなるおそれ
がある。本発明の目的は、スクラップ予熱装置での有機
塩素化合物の発生自体を低減できる電気炉排ガス処理方
法を提供することにある。
Conventionally, it can be said that the generation of the organic chlorine compound in the scrap preheating device is allowed and the trapping efficiency after the generation is improved. However, when a large amount of dust containing vinyl chloride and processing oil containing extreme pressure additives are present in the raw material scrap, the generation of organochlorine compounds in the scrap preheating device will increase accordingly, and only the capture efficiency will be improved. May not be able to deal with it. An object of the present invention is to provide an electric furnace exhaust gas treatment method capable of reducing the generation itself of organic chlorine compounds in a scrap preheating device.

【0004】[0004]

【課題を解決するための手段】上記目的を達成するため
の、本発明に係る電気炉排ガス処理方法は次の方法から
成る。電気炉からの排ガスの少なくとも一部をスクラッ
プ予熱装置に通し、その後排ガスをスプレー冷却塔に通
し、その後排ガスをバグ集塵機に通す電気炉排ガス処理
方法において、前記スクラップ予熱装置内に、アルカリ
およびアルカリ土類から選択された少なくとも一種の元
素の塩を添加しておき、ついで電気炉からの排ガスを前
記スクラップ予熱装置に通す電気炉排ガス処理方法。
In order to achieve the above object, an electric furnace exhaust gas treatment method according to the present invention comprises the following methods. At least a part of the exhaust gas from the electric furnace is passed through a scrap preheating device, then the exhaust gas is passed through a spray cooling tower, and then the exhaust gas is passed through a bag dust collector, in the scrap preheating device, alkali and alkaline earth An electric furnace exhaust gas treatment method, wherein a salt of at least one element selected from the group is added, and then the exhaust gas from the electric furnace is passed through the scrap preheating device.

【0005】[0005]

【作用】上記本発明の方法では、スクラップ予熱装置内
で、スクラップ中に含まれている、塩化ビニルや極圧添
加剤を含む加工油等が、電気炉からの高温排ガスに触れ
て熱分解したときに塩素を生じるが、該塩素は添加され
ているアルカリあるいはアルカリ土類の塩と化学反応を
生じてアルカリあるいはアルカリ土類の塩化物となって
固定化され、有機塩素化合物の生成が抑えられ、有機塩
素化合物の系外への排出も問題なくなる。
In the above method of the present invention, in the scrap preheating device, the processing oil containing vinyl chloride and the extreme pressure additive contained in the scrap is thermally decomposed by touching the high temperature exhaust gas from the electric furnace. Occasionally, chlorine is produced, but the chlorine chemically reacts with the added salt of alkali or alkaline earth to be fixed as chloride of alkali or alkaline earth, and is immobilized, and formation of organic chlorine compound is suppressed. Also, there is no problem in discharging organic chlorine compounds out of the system.

【0006】[0006]

【実施例】図1は電気炉の排ガス処理装置を示してい
る。電気炉1には燃焼塔2が接続され、燃焼塔2にはス
クラップ予熱装置3とガスクーラ4の並列経路が接続さ
れている。スクラップ予熱装置3の下流にはブロワ5が
設けられる。この並列経路は再び合流して、その合流経
路にダスト沈降塔6が接続されている。沈降塔6はメイ
ンブロワ7に接続され、メインブロワ7はスプレー冷却
塔8に接続されている。スプレ冷却塔8に対してバイパ
ス経路が設けられる。スプレー冷却塔8を通る経路とバ
イパス経路とは再び合流し、この合流経路にバグ集塵機
9が接続されている。
EXAMPLE FIG. 1 shows an exhaust gas treatment apparatus for an electric furnace. A combustion tower 2 is connected to the electric furnace 1, and a parallel path of a scrap preheating device 3 and a gas cooler 4 is connected to the combustion tower 2. A blower 5 is provided downstream of the scrap preheating device 3. The parallel paths merge again, and the dust settling tower 6 is connected to the merged path. The settling tower 6 is connected to a main blower 7, and the main blower 7 is connected to a spray cooling tower 8. A bypass path is provided for the spray cooling tower 8. The path passing through the spray cooling tower 8 and the bypass path join again, and the bag dust collector 9 is connected to this joining path.

【0007】電気炉1からの排ガスは燃焼塔2に導か
れ、未燃成分が完成燃焼される。この排ガスは高温で大
きな熱エネルギをもっているので、電気炉1に投入され
るスクラップの予熱に利用するために、排ガスの少なく
とも一部はスクラップ予熱装置3に通される。スクラッ
プの中には、廃自動車のシュレッダスクラップのよう
に、塩化ビニル(電線の被覆材等)や、シュレッダから
の極圧添加剤を含む切削油などの機械加工油が存在す
る。これらは、排ガスの熱で分解されて、塩素を生成
し、通常HCl(塩化水素)の蒸気の形をとる。スクラ
ップ予熱装置3に通された排ガスはスクラップを予熱
し、自身はスクラップにより温度をさげられる。ガスク
ーラ4側に通された排ガスはガスクーラ4で温度をさげ
られる。排ガスは、なお多量をダストを含んでいるの
で、ダスト沈降塔で比重の差を利用してダストをガスか
ら分離し、沈降させる。排ガスはさらにメインブロワ7
で吸引されて、スプレー塔8に送られ、そこで水スプレ
ーを排ガスにかけて、排ガスを洗浄するとともに、排ガ
ス温度をさげる。排ガス中の有機成分は凝縮して洗浄さ
れたり、ダストに吸着されて除去される。最後に、排ガ
スはバグ集塵機9に通され、バグフィルタで、残ってい
るダストや凝縮有機成分を除去し、その後大気に放出さ
れる。
The exhaust gas from the electric furnace 1 is guided to the combustion tower 2 and the unburned components are completely burned. Since the exhaust gas has a large amount of heat energy at a high temperature, at least a part of the exhaust gas is passed through the scrap preheating device 3 in order to be used for preheating the scrap put into the electric furnace 1. Among the scraps, there is a machining oil such as a cutting oil containing vinyl chloride (a covering material for electric wires, etc.) and an extreme pressure additive from the shredder, like shredder scrap of an abandoned automobile. These are decomposed by the heat of exhaust gas to produce chlorine, usually in the form of HCl (hydrogen chloride) vapor. The exhaust gas passed through the scrap preheating device 3 preheats the scrap, and the temperature of the scrap itself is lowered by the scrap. The temperature of the exhaust gas passed through the gas cooler 4 side can be reduced by the gas cooler 4. Since the exhaust gas still contains a large amount of dust, the dust is separated from the gas and settled by utilizing the difference in specific gravity in the dust settling tower. Exhaust gas is further main blower 7
And is sent to a spray tower 8 where a water spray is applied to the exhaust gas to wash the exhaust gas and reduce the exhaust gas temperature. Organic components in exhaust gas are condensed and washed, or are adsorbed by dust and removed. Finally, the exhaust gas is passed through a bag dust collector 9 to remove remaining dust and condensed organic components by a bag filter, and then released to the atmosphere.

【0008】上記において、スクラップ予熱装置3の蓋
を開けて製鋼用スクラップをスクラップ予熱装置3に投
入するときに、スクラップ予熱装置3内に、アルカリお
よびアルカリ土類から選択された少なくとも一種以上の
元素の塩10を添加する。その後、蓋を閉めてスクラッ
プ予熱装置3に電気炉1からの排ガスを通す。
In the above, when the scrap preheating device 3 is opened and the steelmaking scrap is fed into the scrap preheating device 3, at least one or more elements selected from alkali and alkaline earth are contained in the scrap preheating device 3. Salt 10 is added. Then, the lid is closed and the exhaust gas from the electric furnace 1 is passed through the scrap preheating device 3.

【0009】上記のうち、アルカリ元素としては、たと
えばNa、Kなどがあり、その塩はたとえばNa2 CO
3 、K2 CO3 などである。また、アルカリ土類元素と
しては、たとえばCa、Mgがあり、その塩は、たとえ
ばCaO、Ca(OH)2 、CaCO3 、MgO、Mg
(OH)2 、MgCO3 などである。上記塩の添加方法
は、スクラップに混入する方法、スクラップ予熱装置下
部に敷きつめる方法、スクラップ上部を覆うように敷き
つめる方法、スクラップと塩を交互に投入していく方
法、などの何れでもよい。
Of the above, the alkali elements include, for example, Na and K, and the salts thereof are, for example, Na 2 CO.
3 , K 2 CO 3, etc. Examples of alkaline earth elements include Ca and Mg, and salts thereof include CaO, Ca (OH) 2 , CaCO 3 , MgO and Mg.
(OH) 2 , MgCO 3 and the like. The salt addition method may be any of a method of mixing in scrap, a method of spreading the scrap under the preheating device, a method of spreading the scrap so as to cover the upper portion, and a method of alternately charging scrap and salt.

【0010】排ガスを通してスクラップ中に上記の如く
塩素が生成し、Cl2 、HClの形で浮遊すると、これ
ら塩素、塩化水素は、添加剤であるアルカリ、アルカリ
土類の、塩と反応して、NaCl、CaCl2 、MgC
2 等の安定度の大きい塩化物を生成し、塩素成分を固
定化する。したがって、ガス中の塩素成分が有機成分と
再結合して有機塩素化合物を生成することが抑制され
る。すなわち、塩素成分は有機成分と結合するよりも、
アルカリ、アルカリ土類の塩と、化学反応を生じて塩素
化合物になろうとし、有機塩素化合物の生成がそれだけ
抑制される。したがって、バグ集塵機9を通して系外に
排出される有機塩素化合物の量も少なくなる。
When chlorine is generated in the scrap through the exhaust gas as described above and floats in the form of Cl 2 and HCl, these chlorine and hydrogen chloride react with the salts of the alkali, alkaline earth and the additives, NaCl, CaCl 2 , MgC
It produces chloride with high stability such as l 2 and immobilizes the chlorine component. Therefore, it is possible to prevent the chlorine component in the gas from recombining with the organic component to form an organic chlorine compound. That is, the chlorine component is more
Attempts to form a chlorine compound by chemically reacting with an alkali salt or an alkaline earth salt, so that the production of an organic chlorine compound is suppressed to that extent. Therefore, the amount of the organic chlorine compound discharged outside the system through the bag dust collector 9 also decreases.

【0011】上記の塩素成分の固定化の確認試験を、図
2の机上装置による試験と、図1の実機による試験との
それぞれで行った。図2の装置の机上試験では、加熱可
能の管状炉11内に塩化ビニル(所定塩素当量)と固定
化剤との、表1に示した混合物を入れ、加熱温度と混合
化を種々に変えて、試験を行い、管状炉11からの排ガ
スをポンプ12で吸った。固定化剤によって固定された
塩素量は管状炉11内の混合物を取り出し、水に溶か
し、成分を分析して求めた。塩の形で存在するので水に
溶かして残留可溶性塩素量を測定できる。一方、固定化
剤によって固定されずに揮発した塩素量(塩化水素の形
で存在)は、管状炉11とポンプ12との間の経路に吸
収瓶13を設置して塩化水素を捕捉した。塩化水素は水
に容易に溶けるので、吸収瓶13の中に水を入れてお
き、それに管状炉11からの排ガスを通し、塩化水素を
吸収した水を分析するかまたはそのPHをはかって捕捉
塩素量を測定した。結果を表1に示す。
The confirmation test of the immobilization of the chlorine component was carried out in each of the test by the desktop device in FIG. 2 and the test by the actual device in FIG. In the desk test of the apparatus of FIG. 2, the mixture shown in Table 1 of vinyl chloride (predetermined chlorine equivalent) and the immobilizing agent was put in a heatable tubular furnace 11 and various heating temperatures and mixing were changed. The test was conducted, and the exhaust gas from the tubular furnace 11 was sucked by the pump 12. The amount of chlorine fixed by the fixing agent was determined by taking out the mixture in the tubular furnace 11, dissolving it in water, and analyzing the components. Since it exists in the form of salt, it can be dissolved in water to measure the amount of residual soluble chlorine. On the other hand, the amount of volatile chlorine (present in the form of hydrogen chloride) that was not fixed by the fixing agent was set in the absorption bottle 13 in the path between the tubular furnace 11 and the pump 12 to capture hydrogen chloride. Since hydrogen chloride is easily dissolved in water, water is put in the absorption bottle 13 and the exhaust gas from the tubular furnace 11 is passed through it to analyze the hydrogen chloride-absorbed water or measure its PH to capture chlorine. The quantity was measured. The results are shown in Table 1.

【0012】[0012]

【表1】 [Table 1]

【0013】表1からわかることは、塩化ビニルの熱分
解は約600°C近傍で最大となり、アルカリ土類の塩
との反応により、約600°C近傍で80%以上を固定
化できる。また、塩素の固定にはアルカリの塩よりアル
カリ土類の塩の方が効果が大である。また、固定化剤を
増量すれば、それだけ塩素の固定化は促進される。
It can be seen from Table 1 that the thermal decomposition of vinyl chloride is maximized at around 600 ° C, and 80% or more can be fixed around 600 ° C by the reaction with the salt of alkaline earth. In addition, alkaline earth salts are more effective than chlorine salts in fixing chlorine. Further, the more immobilization agent, the more the immobilization of chlorine is promoted.

【0014】図1の装置による実機試験では、スクラッ
プ予熱装置に、70トンのスクラップに対して50−2
00KgのCa(OH)2 を添加し、操業した。バグフ
ィルタ直前において、クロロフェノール、クロロベンゼ
ン類の測定を行った結果、いずれもCa(OH)2 を添
加しない場合に比べ捕捉塩素量は1/10以下に低下し
た。したがって、排出塩素量も1/10以下になること
が判明した。
In the actual machine test by the apparatus shown in FIG. 1, the scrap preheater is 50-2 for 70 tons of scrap.
00 Kg of Ca (OH) 2 was added and operation was carried out. As a result of measuring chlorophenol and chlorobenzene immediately before the bag filter, the amount of scavenged chlorine was reduced to 1/10 or less as compared with the case where Ca (OH) 2 was not added. Therefore, it was found that the amount of discharged chlorine was 1/10 or less.

【0015】[0015]

【発明の効果】本発明によれば、スクラップ予熱装置内
にアルカリおよびアルカリ土類から選択された少なくと
も1種以上の元素の塩を添加して、排ガスを通すように
したので、排ガスの熱によってスクラップ中の塩化ビニ
ル等が熱分解したときに生成する塩素、塩化水素を上記
塩と反応させて塩化物として固定化することができ、有
機塩素化合物がスクラップ予熱装置内で生成されること
を抑制でき、系外への排出も抑制できる。
According to the present invention, a salt of at least one element selected from alkali and alkaline earth elements is added to the scrap preheating device so that the exhaust gas can pass therethrough. Chlorine and hydrogen chloride generated when vinyl chloride, etc. in scrap is thermally decomposed can be fixed as chloride by reacting with the above salts, suppressing the generation of organic chlorine compounds in the scrap preheater. It is possible to suppress the discharge to the outside of the system.

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

【図1】電気炉の排ガス処理装置の系統図である。FIG. 1 is a system diagram of an exhaust gas treatment device of an electric furnace.

【図2】本発明の方法の机上試験を実施する装置の系統
図である。
FIG. 2 is a systematic diagram of an apparatus for carrying out a desk test of the method of the present invention.

【符号の説明】[Explanation of symbols]

1 電気炉 3 スクラップ予熱装置 1 Electric furnace 3 Scrap preheater

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 電気炉からの排ガスの少なくとも一部を
スクラップ予熱装置に通し、その後排ガスをスプレー冷
却塔に通し、その後排ガスをバグ集塵機に通す電気炉排
ガス処理方法において、前記スクラップ予熱装置内に、
アルカリおよびアルカリ土類から選択された少なくとも
一種の元素の塩を添加しておき、ついで電気炉からの排
ガスを前記スクラップ予熱装置に通すことを特徴とする
電気炉排ガス処理方法。
1. An electric furnace exhaust gas treatment method in which at least a part of exhaust gas from an electric furnace is passed through a scrap preheater, then the exhaust gas is passed through a spray cooling tower, and then the exhaust gas is passed through a bag dust collector, in the scrap preheater. ,
An electric furnace exhaust gas treatment method comprising adding a salt of at least one element selected from alkali and alkaline earth and then passing the exhaust gas from the electric furnace through the scrap preheating device.
JP5292226A 1993-11-22 1993-11-22 Exhaust gas treating method for electric furnace Pending JPH07146082A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5292226A JPH07146082A (en) 1993-11-22 1993-11-22 Exhaust gas treating method for electric furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5292226A JPH07146082A (en) 1993-11-22 1993-11-22 Exhaust gas treating method for electric furnace

Publications (1)

Publication Number Publication Date
JPH07146082A true JPH07146082A (en) 1995-06-06

Family

ID=17779132

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5292226A Pending JPH07146082A (en) 1993-11-22 1993-11-22 Exhaust gas treating method for electric furnace

Country Status (1)

Country Link
JP (1) JPH07146082A (en)

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Publication number Priority date Publication date Assignee Title
JP2020536213A (en) * 2017-09-22 2020-12-10 シーアイエスディーアイ エンジニアリング カンパニー リミテッドCisdi Engineering Co., Ltd Horizontal continuous supply preheating device and its enhanced preheating method
CN112892141A (en) * 2021-01-21 2021-06-04 韩占卫 Multi-element dust purification equipment in factory

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2020536213A (en) * 2017-09-22 2020-12-10 シーアイエスディーアイ エンジニアリング カンパニー リミテッドCisdi Engineering Co., Ltd Horizontal continuous supply preheating device and its enhanced preheating method
CN112892141A (en) * 2021-01-21 2021-06-04 韩占卫 Multi-element dust purification equipment in factory

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