JPH0842980A - Method of treating exhaust gas from electric furnace or scrap preheating device for electric furnace - Google Patents

Method of treating exhaust gas from electric furnace or scrap preheating device for electric furnace

Info

Publication number
JPH0842980A
JPH0842980A JP22078594A JP22078594A JPH0842980A JP H0842980 A JPH0842980 A JP H0842980A JP 22078594 A JP22078594 A JP 22078594A JP 22078594 A JP22078594 A JP 22078594A JP H0842980 A JPH0842980 A JP H0842980A
Authority
JP
Japan
Prior art keywords
exhaust gas
electric furnace
harmful components
filter
cooling
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
JP22078594A
Other languages
Japanese (ja)
Other versions
JP3072457B2 (en
Inventor
Makoto Takahashi
誠 高橋
Isao Arimitsu
功 有光
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 JP22078594A priority Critical patent/JP3072457B2/en
Publication of JPH0842980A publication Critical patent/JPH0842980A/en
Application granted granted Critical
Publication of JP3072457B2 publication Critical patent/JP3072457B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Landscapes

  • Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
  • Treating Waste Gases (AREA)

Abstract

(57)【要約】 【目的】 本発明は、材料の溶解中・昇温中の電気炉あ
るいは材料を予熱中のスクラップ予熱装置または電気炉
から発生する排ガス中に含まれる白煙、あるいは悪臭等
の有害成分を安全に除去できるプロセスの提供を目的と
する。 【構成】 排ガスを有害成分が固化する50℃以下の低
温度域まで短時間で冷却する冷却装置4と、この固化し
た有害成分を捕集するための多孔質樹脂材料11からな
る集塵フィルター7で処理設備を構成することにより、
フィルターを結露水等によって目詰まりして使用不能と
することなく、排ガス中の悪臭等の有害成分を初期含有
レベルの1/500〜1/1000程度まで低減可能と
なる。
(57) [Abstract] [Purpose] The present invention is directed to an electric furnace during melting / heating of a material, a scrap preheating device for preheating the material, or white smoke contained in exhaust gas generated from the electric furnace, a foul odor, or the like. The aim is to provide a process that can safely remove harmful components of. [Structure] A cooling device 4 for cooling exhaust gas in a short time to a low temperature region of 50 ° C. or lower where harmful components are solidified, and a dust collecting filter 7 made of a porous resin material 11 for collecting the solidified harmful components. By configuring the processing equipment with
It is possible to reduce harmful components such as malodor in exhaust gas to about 1/500 to 1/1000 of the initial content level without making the filter unusable by clogging with dew condensation water or the like.

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、金属材料を溶解あるい
は精錬する電気炉から溶解・精錬・焦熱中に発生する排
ガス、或いは、金属材料を電気炉内又はスクラップ予熱
専用装置にて予熱するときに発生する排ガス中に含まれ
る有害成分を除去する方法に関する。
BACKGROUND OF THE INVENTION The present invention relates to an exhaust gas generated during melting, refining, and pyroheating from an electric furnace for melting or refining a metal material, or for preheating a metal material in an electric furnace or in a device for exclusive use of scrap preheating. The present invention relates to a method for removing harmful components contained in exhaust gas generated in the air.

【0002】[0002]

【従来の技術】金属材料を電気炉内で溶解、昇温する場
合、あるいは、電気炉内またはスクラップ予熱専用装置
にて予熱する場合、白煙、あるいは悪臭等の有害成分が
発生して問題となっている。この白煙は、金属材料に付
着している油分が蒸発してミスト状になったもので、集
塵装置内の濾布の目詰まり、あるいは火災の原因にな
る。また、悪臭等の有害物質については、そこに就業す
る作業者の作業環境の悪化だけでなく、地域住民の生活
環境にも重大な影響を与える。
2. Description of the Related Art When a metal material is melted and heated in an electric furnace, or preheated in an electric furnace or in a scrap preheating dedicated device, harmful components such as white smoke or a foul odor are generated, which causes a problem. Has become. This white smoke is a mist formed by evaporation of oil adhering to the metal material, which may cause clogging of the filter cloth in the dust collector or a fire. In addition, harmful substances such as foul odors not only worsen the working environment of workers who work there, but also seriously affect the living environment of local residents.

【0003】これら排ガス中に含まれる白煙、あるいは
悪臭等の有害成分を除去する方法として様々な方法が提
案されている。例えば、特開平2−136693号公報
によれば、スクラップ予熱装置から排出される白煙、あ
るいは悪臭等の有害成分を含むガスを、直接水洗式のス
プレー冷却塔で80℃まで冷却することにより、濾布を
燃やすことなくガス中に含まれる白煙、あるいは悪臭等
の有害成分を除去できるとしている。
Various methods have been proposed as methods for removing white smoke contained in these exhaust gases or harmful components such as malodors. For example, according to JP-A-2-136693, white smoke discharged from a scrap preheating device or a gas containing a harmful component such as a foul odor is directly cooled to 80 ° C. by a water-washing type spray cooling tower. It is said that it is possible to remove harmful components such as white smoke or foul odor contained in the gas without burning the filter cloth.

【0004】[0004]

【発明が解決しようとする課題】ところがこの方法だ
と、直接水洗式のスプレー冷却塔で排ガスを冷却するた
めに、集塵装置に入ってくる排ガス中の水蒸気量が極端
に多くなり、濾布表面への結露水の付着が避けられなく
なる。濾布表面に水が付着すると、水は内部に浸透して
除去困難となったり、また、水が濾布表面に捕集された
ダストに吸収されることでダストが固まり、ダストを濾
布表面から払い落とすことが不可能、すなわち、完全に
目詰まりした状態になってくる。このようにフィルター
が目詰まりすると、フィルターを通過するガスの圧力損
失が増加するため、結果的に集塵ガス量が減少し、集塵
効率が悪化してくることとなる。従って、通常3〜5年
で交換する濾布をわずか数カ月で交換することを余儀な
くされる。
With this method, however, the amount of water vapor in the exhaust gas entering the dust collector becomes extremely large because the exhaust gas is cooled directly in the water washing type spray cooling tower, and the filter cloth It becomes unavoidable that dew condensation water adheres to the surface. When water adheres to the surface of the filter cloth, the water permeates inside and becomes difficult to remove, and when water is absorbed by the dust collected on the surface of the filter cloth, the dust is hardened and the dust is removed from the surface of the filter cloth. It is impossible to wipe it off, that is, it becomes completely clogged. When the filter is clogged in this way, the pressure loss of the gas passing through the filter increases, and as a result, the amount of dust collecting gas decreases and the dust collecting efficiency deteriorates. Therefore, the filter cloth, which is normally replaced in 3 to 5 years, is forced to be replaced in only a few months.

【0005】また、金属材料を電気炉内で溶解、昇温す
る場合、あるいは、電気炉内またはスクラップ予熱専用
装置にて予熱する場合に発生する排ガスのように、油分
を多量に含有している場合は、冷却温度が80℃までで
は、悪臭等の有害成分の除去には不充分な温度である。
そこで、本発明では、材料の溶解中・昇温中の電気炉、
あるいは、材料を予熱中のスクラップ予熱装置または電
気炉から発生する排ガス中に含まれる白煙、あるいは悪
臭等の有害成分を、集塵機内の濾布を結露水によって使
用不能にする事なく、確実に除去できる排ガスの処理方
法を提供しようとするものである。
Further, a large amount of oil is contained, such as exhaust gas generated when melting and raising the temperature of a metal material in an electric furnace, or when preheating in an electric furnace or in a scrap preheating dedicated device. In this case, when the cooling temperature is up to 80 ° C., the temperature is insufficient for removing harmful components such as a bad odor.
Therefore, in the present invention, an electric furnace during melting / heating of the material,
Alternatively, it is possible to ensure that white smoke contained in the exhaust gas generated from the scrap preheating device or the electric furnace during preheating of the material, or harmful components such as a bad odor, without making the filter cloth in the dust collector unusable by dew condensation water. It is intended to provide a method for treating exhaust gas that can be removed.

【0006】[0006]

【課題を解決するための手段】上記問題を解決するため
に、本発明における排ガスの処理方法は、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の処理方法で
あって、排ガスを冷却する冷却装置により、前記排ガス
を50℃以下の低温域まで冷却し、次いで前記排ガスを
多孔質樹脂材料からなる集塵フィルターに前記排ガスを
通過せしめることにより有害成分を捕集することを特徴
とする電気炉または電気炉用スクラップ予熱装置からの
排ガスの処理方法である。
In order to solve the above problems, a method for treating exhaust gas according to the present invention is a method for treating exhaust gas from an electric furnace or a scrap preheating device for an electric furnace, which cools exhaust gas. An electric furnace characterized in that the exhaust gas is cooled to a low temperature region of 50 ° C. or lower by an apparatus, and then the exhaust gas is passed through a dust collecting filter made of a porous resin material to collect harmful components. Alternatively, it is a method of treating exhaust gas from the scrap preheating device for an electric furnace.

【0007】また、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の処理方法であって、排ガスを冷却
する冷却装置により、前記排ガスを50℃以下の低温度
まで冷却し、次いで該冷却後の排ガス中に消石灰等の吸
着剤を混入せしめ、さらに、多孔質樹脂材料からなる集
塵フィルターに前記排ガスを通過せしめることにより有
害成分を捕集することを特徴とする電気炉または電気炉
用スクラップからの排ガスの処理方法とすることであ
る。
A method for treating exhaust gas from an electric furnace or a scrap preheating device for an electric furnace, wherein the exhaust gas is cooled to a low temperature of 50 ° C. or lower by a cooling device for cooling the exhaust gas, and then, after the cooling. From scraps for electric furnaces or electric furnaces characterized by collecting harmful components by mixing an adsorbent such as slaked lime in the exhaust gas, and further allowing the exhaust gas to pass through a dust collection filter made of a porous resin material. The exhaust gas treatment method of

【0008】[0008]

【作用】材料の溶解中・昇温中の電気炉、あるいは、材
料を予熱中のスクラップ予熱装置または電気炉から発生
する排ガスには油分が多量に含有している。このような
油分との共存状態においては、悪臭等の有害成分の融点
はその単体で存在するときよりもかなり低く、50℃程
度であることを発明者らは確認している。
A large amount of oil is contained in the exhaust gas generated from the electric furnace during melting / heating of the material, or the scrap preheating device or the electric furnace during preheating of the material. The inventors have confirmed that in the coexistence state with such an oil component, the melting point of harmful components such as malodor is considerably lower than that when it is present alone, and is about 50 ° C.

【0009】従って、上記排ガスを、冷却装置にて50
℃以下の低温域まで短時間で冷却することにより、悪臭
等の有害成分を固化させることができる。これによっ
て、排ガス中の有害成分はそのほとんどすべてが排ガス
中に含まれるダストと供に集塵機にて捕集され、大気に
放出されることはなくなるわけである。
Therefore, the above exhaust gas is cooled by the cooling device.
By cooling to a low temperature range of ℃ or less in a short time, harmful components such as malodor can be solidified. As a result, almost all of the harmful components in the exhaust gas are collected by the dust collector together with the dust contained in the exhaust gas and are not released to the atmosphere.

【0010】また、集塵フィルターは、表面にフッ素ま
たはシリコン含有の多孔質樹脂材料を被覆した連通多孔
質樹脂材料から構成されている。通常の織物である濾布
の空隙は80μm程度であるのに対し、このフィルター
表面の空隙は4μm程度であるため、例えばフィルター
表面に結露した水分はフィルター内部に浸透することが
ない。従って、そのまま表面にとどまり、捕集されたダ
ストと供にそのまま下に流れ降りるため、目詰まり等で
フィルターを使用不能にすることはなくなる。従って、
フィルターの寿命は、従来の3〜5か月と同等にとどま
ることなく、従来より寿命は更に伸びることになる。
Further, the dust collecting filter is composed of a continuous porous resin material having a surface coated with a porous resin material containing fluorine or silicon. The filter cloth, which is a normal woven fabric, has pores of about 80 μm, whereas the pores of the filter surface are about 4 μm, so that, for example, water condensed on the filter surface does not penetrate into the filter. Therefore, since it stays on the surface as it is and flows down downward together with the collected dust, the filter is not disabled due to clogging or the like. Therefore,
The life of the filter does not remain the same as the conventional 3 to 5 months, and the life is further extended from the conventional one.

【0011】また更に、消石灰等を吸着剤供給装置から
排ガス中に吹き込むことにより悪臭等の有害成分を吸着
させ、その後、集塵フィルターにて排ガス中のダストと
供に吹き込んだ消石灰等を捕獲する。このプロセスによ
って、悪臭等の有害成分の捕集効率は更に向上する。
尚、集塵フィルターにて捕獲されたダスト、あるいは、
ダストと混合した粉状の消石灰等は、粒状に成形し、電
気炉内に戻して溶解することによって、排気等の処理が
不要となり、二次公害を防止できる。
Furthermore, slaked lime or the like is blown into the exhaust gas from the adsorbent supply device to adsorb harmful components such as a bad odor, and then the slaked lime or the like blown together with the dust in the exhaust gas is captured by the dust collecting filter. . By this process, the collection efficiency of harmful components such as malodor is further improved.
In addition, the dust captured by the dust collection filter, or
Powdered slaked lime or the like mixed with dust is shaped into particles, and returned to the electric furnace to be melted, so that processing such as exhaust is unnecessary, and secondary pollution can be prevented.

【0012】[0012]

【実施例】以下、本発明による実施例を図面により、詳
細に説明する。図1は本発明に係る基本プロセスの装置
構成図であり、吸着剤供給装置を有する例を示す。これ
は、電気炉における金属材料の予熱、溶解、あるいは昇
温中に発生する排ガス中に含まれる白煙、あるいは悪臭
等の有害成分を分解除去するプロセスを示す。
Embodiments of the present invention will now be described in detail with reference to the drawings. FIG. 1 is a device configuration diagram of a basic process according to the present invention, showing an example having an adsorbent supply device. This shows a process of decomposing and removing harmful components such as white smoke or foul odor contained in exhaust gas generated during preheating, melting, or temperature rise of a metal material in an electric furnace.

【0013】電気炉1から発生する排ガスはダクト2を
通って燃焼塔3に導入される。ここで排ガス中に含まれ
るCOガスが燃焼され、それとともに、排ガス中に含ま
れる白煙、悪臭等の一部は加熱分解される。燃焼塔3を
出た排ガスは、冷却装置4に導入される。ここで、例え
ばスプレーノズル5より噴霧される水の噴霧粒子によっ
て排ガスは50℃以下まで直接冷却される。一度、燃焼
加熱によって分解された悪臭等は、300℃雰囲気にて
ある期間保持されると再生成するため、ここでは水によ
る直接冷却によって短時間に急激に冷却する。
Exhaust gas generated from the electric furnace 1 is introduced into the combustion tower 3 through the duct 2. Here, CO gas contained in the exhaust gas is burned, and at the same time, part of white smoke, malodor, etc. contained in the exhaust gas is thermally decomposed. The exhaust gas leaving the combustion tower 3 is introduced into the cooling device 4. Here, the exhaust gas is directly cooled to 50 ° C. or lower by spray particles of water sprayed from the spray nozzle 5, for example. The malodor and the like once decomposed by combustion heating are regenerated when kept in an atmosphere of 300 ° C. for a certain period of time, and therefore, the water is directly cooled by water to rapidly cool it in a short time.

【0014】ここでは、冷却方法として1つの冷却装置
内での水噴霧による冷却の例を述べたが、冷却装置は1
つに限定されることなく複数でも良く、また、水噴霧以
外に水冷ダクト、空冷ダクト、熱交換装置等の冷却装置
を用いて良いことはもちろんである。吸着剤供給装置6
によって排ガス中に消石灰等の粉体を吹き込み、残留し
た悪臭等の有害成分を吸着させる。ここで、排ガス中に
吹き込む粉体としては、消石灰の他、チャー、石炭灰、
活性炭、尿素等でも良い。この吹き込んだ消石灰等は、
排ガス中のダストと共に集塵フィルター7にて捕獲さ
れ、スタック8により大気中に放散される排ガス中の悪
臭等の有害成分レベルは、初期の1/500〜1/10
00程度まで低減される。集塵フィルター7にて捕獲さ
れたダストあるいはダストを含んだ消石灰等は、ペレタ
イザー9に送られ粒状化され再び電気炉1に投入されて
溶解される。従って、廃棄等の処理が不要となり、二次
公害を防止できる。
Here, an example of cooling by water spray in one cooling device has been described as the cooling method.
Of course, the number is not limited to one, and a plurality of cooling devices may be used, and in addition to the water spray, cooling devices such as a water cooling duct, an air cooling duct, and a heat exchange device may be used. Adsorbent supply device 6
By blowing powder such as slaked lime into the exhaust gas, the residual harmful components such as bad odor are adsorbed. Here, as the powder blown into the exhaust gas, in addition to slaked lime, char, coal ash,
Activated carbon, urea, etc. may be used. This blown slaked lime, etc.
The level of harmful components such as a foul odor in the exhaust gas that is captured by the dust collection filter 7 together with the dust in the exhaust gas and is diffused into the atmosphere by the stack 8 is 1/500 to 1/10 of the initial level.
It is reduced to about 00. Dust or slaked lime containing dust captured by the dust collecting filter 7 is sent to the pelletizer 9, is granulated, and is thrown into the electric furnace 1 again to be melted. Therefore, disposal such as disposal becomes unnecessary and secondary pollution can be prevented.

【0015】図2は、本発明に係る集塵フィルターの断
面図を示す。フィルターは、空隙40〜60μm程度の
連通多孔質樹脂材料の母材10の表面に、空隙4μm程
度のフッ素またはシリコン含有の多孔質樹脂材料11を
被覆した構造となっている。ガスは、多孔質樹脂材料を
被覆したA方向からフィルター内に侵入し、内部空間1
2を通過してフィルター外へ出る。ダスト及び水分は、
ガスがA方向からフィルター内に侵入する前に、多孔質
樹脂材料11の表面に捕捉される。
FIG. 2 shows a sectional view of the dust collecting filter according to the present invention. The filter has a structure in which the surface of a base material 10 of a continuous porous resin material having a gap of about 40 to 60 μm is covered with a porous resin material 11 containing fluorine or silicon having a gap of about 4 μm. The gas penetrates into the filter from the direction A covered with the porous resin material, and the internal space 1
Pass 2 and go out of the filter. Dust and moisture are
Before the gas enters the filter from the A direction, it is captured on the surface of the porous resin material 11.

【0016】[0016]

【発明の効果】本発明プロセスによって、電気炉におけ
る金属材料の予熱、溶解、あるいは昇温中に発生する排
ガス中に含まれる悪臭等の有害成分を、発生する量の1
/500〜1/1000にまで低減することが可能とな
る。また、フィルターの寿命は、従来と同等にとどまる
だけでなく、従来より寿命は更に伸びることとなる。従
って、フィルターのランニングコストも大幅に低減され
ることとなる。このように、排ガス中の有害成分のほと
んどすべてを、大気中に放出することなく、集塵機での
捕集が可能になると共に、この集塵機で捕集したダスト
及びダストとの混合物は、電気炉に戻して再溶解するこ
とにより、廃棄物の処理が不要となり、二次公害も防止
できるという優れた効果を奏するものである。
According to the process of the present invention, the amount of harmful components such as malodor contained in exhaust gas generated during preheating, melting, or temperature rise of a metal material in an electric furnace can be reduced to 1
It is possible to reduce to / 500 to 1/1000. Moreover, the life of the filter is not only the same as that of the conventional filter, but also the life of the filter is longer than that of the conventional filter. Therefore, the running cost of the filter can be significantly reduced. In this way, almost all of the harmful components in the exhaust gas can be collected by the dust collector without being released into the atmosphere, and the dust collected by this dust collector and the mixture with the dust can be stored in the electric furnace. By returning and re-dissolving, there is no need to treat waste, and secondary pollution can be prevented, which is an excellent effect.

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

【図1】本発明に係る電気炉における金属材料の予熱、
溶解、あるいは昇温中に発生する排ガス中に含まれる悪
臭等の有害成分を分解除去する基本プロセスの装置構成
図を示す。
FIG. 1 shows preheating of a metal material in an electric furnace according to the present invention,
FIG. 1 shows an apparatus configuration diagram of a basic process for decomposing and removing harmful components such as malodor contained in exhaust gas generated during melting or temperature rise.

【図2】本発明に係る集塵フィルターの断面図を示す。FIG. 2 shows a cross-sectional view of a dust collecting filter according to the present invention.

【符号の説明】[Explanation of symbols]

1 電気炉 2 ダクト 3 燃焼塔 4 冷却装置 5 スプレーノズル 6 吸着剤供給装置 7 集塵フィルター 8 スタック 9 ペレタイザー 10 母材 11 フッ素またはシリコン含有の多孔質樹脂材料 12 内部空間 1 Electric Furnace 2 Duct 3 Combustion Tower 4 Cooling Device 5 Spray Nozzle 6 Adsorbent Supply Device 7 Dust Collection Filter 8 Stack 9 Pelletizer 10 Base Material 11 Fluorine- or Silicon-Containing Porous Resin Material 12 Internal Space

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C21C 5/52 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display location C21C 5/52

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
からの排ガスの処理方法であって、排ガスを冷却する冷
却装置により、前記排ガスを50℃以下の低温域まで冷
却し、次いで前記排ガスを多孔質樹脂材料からなる集塵
フィルターに前記排ガスを通過せしめることにより有害
成分を捕集することを特徴とする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の処理方法。
1. A method for treating exhaust gas from an electric furnace or a scrap preheating device for an electric furnace, wherein the exhaust gas is cooled to a low temperature region of 50 ° C. or lower by a cooling device for cooling the exhaust gas, and then the exhaust gas is porous. A method for treating exhaust gas from an electric furnace or a scrap preheating device for an electric furnace, comprising collecting harmful components by passing the exhaust gas through a dust collecting filter made of a high quality resin material.
【請求項2】電気炉または電気炉用スクラップ予熱装置
からの排ガスの処理方法であって、排ガスを冷却する冷
却装置により、前記排ガスを50℃以下の低温度まで冷
却し、次いで該冷却後の排ガス中に消石灰等の吸着剤を
混入せしめ、さらに、多孔質樹脂材料からなる集塵フィ
ルターに前記排ガスを通過せしめることにより有害成分
を捕集することを特徴とする電気炉または電気炉用スク
ラップからの排ガスの処理方法。
2. A method for treating exhaust gas from an electric furnace or a scrap preheating device for an electric furnace, wherein the exhaust gas is cooled to a low temperature of 50 ° C. or lower by a cooling device for cooling the exhaust gas, and then the cooled exhaust gas is cooled. From scraps for electric furnaces or electric furnaces characterized by collecting harmful components by mixing an adsorbent such as slaked lime in the exhaust gas, and further allowing the exhaust gas to pass through a dust collection filter made of a porous resin material. Exhaust gas treatment method.
JP22078594A 1994-05-23 1994-08-24 Method of treating exhaust gas from electric furnace or scrap preheating device for electric furnace Expired - Fee Related JP3072457B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22078594A JP3072457B2 (en) 1994-05-23 1994-08-24 Method of treating exhaust gas from electric furnace or scrap preheating device for electric furnace

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP13086194 1994-05-23
JP6-130861 1994-05-23
JP22078594A JP3072457B2 (en) 1994-05-23 1994-08-24 Method of treating exhaust gas from electric furnace or scrap preheating device for electric furnace

Publications (2)

Publication Number Publication Date
JPH0842980A true JPH0842980A (en) 1996-02-16
JP3072457B2 JP3072457B2 (en) 2000-07-31

Family

ID=26465875

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22078594A Expired - Fee Related JP3072457B2 (en) 1994-05-23 1994-08-24 Method of treating exhaust gas from electric furnace or scrap preheating device for electric furnace

Country Status (1)

Country Link
JP (1) JP3072457B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115677374A (en) * 2022-11-15 2023-02-03 北京科技大学 A method for condensing wet flue gas in the condensation section of ceramsite roasting kiln

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115677374A (en) * 2022-11-15 2023-02-03 北京科技大学 A method for condensing wet flue gas in the condensation section of ceramsite roasting kiln

Also Published As

Publication number Publication date
JP3072457B2 (en) 2000-07-31

Similar Documents

Publication Publication Date Title
CN101869800A (en) Method and system for purifying flue gas generated by incinerating waste materials
JP2000157832A (en) Waste activated carbon treatment method and activated coke treatment method
CN206944178U (en) A kind of smoke processing system
JP4632374B2 (en) Method and apparatus for removing mercury from incinerated ash containing mercury and apparatus for treating exhaust gas containing mercury
JPH10109016A (en) Treatment of heavy metal-containing waste gas and device therefor
JP3285692B2 (en) Fly ash treatment device in incinerator
JP3072457B2 (en) Method of treating exhaust gas from electric furnace or scrap preheating device for electric furnace
JP4979911B2 (en) Heat purification equipment for contaminated soil
JP4516830B2 (en) Heat purification equipment for contaminated soil
JPH06117780A (en) Equipment for treating exhaust gas from electric furnaces or scrap preheaters for electric furnaces
JP2002263633A (en) Contaminated soil purification equipment
JP4124584B2 (en) Removal method of dioxins in exhaust gas from waste treatment furnace
JP4177995B2 (en) Method for reducing wet dust
JP3343328B2 (en) Apparatus and method for melting wet ash
JPH0718665B2 (en) Exhaust gas treatment device
JPH108118A (en) Method for producing desulfurizing agent for steelmaking from waste incineration exhaust gas
JPH0635888B2 (en) Garbage incineration plant
JPH08285249A (en) Waste treatment method and treatment equipment
JP3966485B2 (en) Method and apparatus for treating exhaust gas generated during incineration of waste containing chlorine compounds
JPH10267256A (en) Method and apparatus for cooling incinerator exhaust gas
JP3866832B2 (en) Method for treating fly ash in exhaust gas in waste treatment equipment
JPH11183051A (en) Exhaust gas treatment method in electric furnace
JP4122570B2 (en) Exhaust gas treatment equipment for arc furnace
JPH09229572A (en) Exhaust gas treatment method in scrap melting
JP2023183540A (en) Exhaust gas treatment equipment and treatment method

Legal Events

Date Code Title Description
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20000328

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313111

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

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

Free format text: PAYMENT UNTIL: 20090602

Year of fee payment: 9

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

Free format text: PAYMENT UNTIL: 20090602

Year of fee payment: 9

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

Free format text: PAYMENT UNTIL: 20100602

Year of fee payment: 10

LAPS Cancellation because of no payment of annual fees