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JP2595590B2 - Exhaust gas treatment method after scrap preheating - Google Patents

Exhaust gas treatment method after scrap preheating

Info

Publication number
JP2595590B2
JP2595590B2 JP31438387A JP31438387A JP2595590B2 JP 2595590 B2 JP2595590 B2 JP 2595590B2 JP 31438387 A JP31438387 A JP 31438387A JP 31438387 A JP31438387 A JP 31438387A JP 2595590 B2 JP2595590 B2 JP 2595590B2
Authority
JP
Japan
Prior art keywords
exhaust gas
scrap
preheating
fuel
tower
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.)
Expired - Lifetime
Application number
JP31438387A
Other languages
Japanese (ja)
Other versions
JPH01155195A (en
Inventor
幸雄 丹羽
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.)
Daido Steel Co Ltd
Original Assignee
Daido Steel Co 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 Daido Steel Co Ltd filed Critical Daido Steel Co Ltd
Priority to JP31438387A priority Critical patent/JP2595590B2/en
Publication of JPH01155195A publication Critical patent/JPH01155195A/en
Application granted granted Critical
Publication of JP2595590B2 publication Critical patent/JP2595590B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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

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

Description

【発明の詳細な説明】 <産業上の利用分野> 本発明はスクラップ予熱後の排ガスの処理方法に関す
る。
The present invention relates to a method for treating exhaust gas after preheating of scrap.

金属溶解に電気炉が広く利用されているが、この種の
電気炉からは、原料をアーク熱により溶解する性質上、
高温の排ガスが発生する。そしてこの排ガスは、燃焼塔
でいわゆる自己燃焼により後燃焼され、更にクーラ及び
最終的には集塵装置を経て無害化された後、大気中へ放
出される。しかし、このような電気炉からの排ガスの顕
熱を特に有効利用することなく大気中へ放出するのでは
熱エネルギの著しい無駄である。
Electric furnaces are widely used for melting metals, but from this kind of electric furnace, due to the property of melting raw materials by arc heat,
Hot exhaust gas is generated. The exhaust gas is post-combusted by a so-called self-combustion in a combustion tower, further detoxified through a cooler and finally through a dust collector, and then released into the atmosphere. However, if the sensible heat of the exhaust gas from such an electric furnace is released into the atmosphere without particularly effective use, heat energy is extremely wasted.

そこで、電気炉からの排ガスの顕熱を原料であるスク
ラップの予熱に利用することが行なわれているが、該ス
クラップが例えばダライ粉やシュレッダ等の低級スクラ
ップである場合には特に、予熱後の排ガス中に、上記低
級スクラップの油分や塗料等に起因する悪臭成分、例え
ば硫化水素やアセトアルデヒド更にはスチレン等が多量
に含まれてくる。かかる悪臭成分は、これをそのまま集
塵装置を経て大気中へ放出すると、該集塵装置へ悪影響
を及ぼし、また重大な二次公害を引き起こすことになる
ので、スクラップ予熱後の排ガスを集塵装置へ導入する
前に、該スクラップ予熱後の排ガス中から悪臭成分を脱
臭しておくことが強く要請される。
Therefore, the sensible heat of the exhaust gas from the electric furnace is used for preheating of the scrap as a raw material. Particularly, when the scrap is a low-grade scrap such as Dalai powder or shredder, particularly after the preheating. The exhaust gas contains a large amount of malodorous components such as hydrogen sulfide, acetaldehyde, and styrene due to the oil content of the low-grade scrap and the paint. If such malodorous components are directly discharged into the atmosphere via a dust collector, they will have an adverse effect on the dust collector and cause serious secondary pollution. It is strongly required to remove odorous components from the exhaust gas after the preheating of the scrap before introducing it into the waste gas.

本発明は、上記要請に応えるもので、特にもともとス
クラップの予熱が電気炉からの排ガスの顕熱を有効利用
しようとする観点に立つものであるから、かかる観点に
逆行することのないよう、できるだけ省エネルギ化され
た条件下でスクラップ予熱後の排ガスを脱臭し、そして
脱臭後の排ガスを集塵装置で処理する方法に関するもの
である。
The present invention responds to the above demand, and in particular, since the preheating of scrap originally takes a viewpoint of effectively utilizing the sensible heat of exhaust gas from an electric furnace, so as not to go back to such a viewpoint, The present invention relates to a method for deodorizing exhaust gas after scrap preheating under energy-saving conditions, and treating the exhaust gas after deodorization with a dust collector.

<従来の技術、その問題点> 従来、スクラップ予熱後の排ガスを脱臭する処理方法
として、該予熱後の排ガスを、電気炉からの排ガスを後
燃焼させるための燃焼塔へ返送することが行なわれてい
る。ところが、この従来法には、燃焼塔内の燃焼雰囲気
が電気炉の操業条件によって大きな影響を受けることも
あって、スクラップ予熱後の排ガス中に含まれる悪臭成
分が該燃焼塔で充分に燃焼(酸化分解)されず、そのま
ま集塵装置へと送出され、更には大気中へと放出されて
しまうことがあるため、該悪臭成分が集塵装置へ悪影響
を及ぼし、また重大な二次公害を引き起こすという問題
点がある。
<Prior art and its problems> Conventionally, as a treatment method for deodorizing exhaust gas after preheating scrap, the exhaust gas after preheating is returned to a combustion tower for post-burning exhaust gas from an electric furnace. ing. However, according to this conventional method, the combustion atmosphere in the combustion tower is greatly affected by the operating conditions of the electric furnace, and the malodorous components contained in the exhaust gas after the preheating of the scrap are sufficiently burned in the combustion tower ( Without being oxidatively decomposed, it may be sent to the dust collector as it is, and may be released to the atmosphere, so that the odorous component has an adverse effect on the dust collector and causes serious secondary pollution. There is a problem.

そこで従来、スクラップ予熱後の排ガスを脱臭する別
の処理方法として、該予熱後の排ガスを、燃焼塔とは別
に分解炉を設置し、該分解炉で燃焼させる方法が提案さ
れている(特開昭56−155379号)。ところが、この従来
法には、スクラップ予熱後の排ガス中に含まれる悪臭成
分の内容(成分の種類や濃度)がスクラップの性状等に
よって大きく変化するにもかかわらず、かかる性状とは
無関係に該スクラップ予熱後の排ガスを分解炉において
燃料により燃焼させるため、該燃料が実際には無駄に使
用されることが多く、したがって電気炉からの排ガスの
顕熱を有効利用してスクラップを予熱するという本来の
目的に大きく相反することになってしまうという問題点
がある。
Therefore, conventionally, as another treatment method for deodorizing the exhaust gas after the preheating of the scrap, a method of installing a decomposition furnace separately from the combustion tower and burning the exhaust gas after the preheating by the decomposition furnace has been proposed (Japanese Patent Application Laid-Open No. H10-163873). No. 56-155379). However, according to this conventional method, despite the fact that the contents (type and concentration of the odor component) contained in the exhaust gas after the preheating of the scrap vary greatly depending on the properties of the scrap, etc., the scrap does not matter. Since the exhaust gas after preheating is burned with fuel in the cracking furnace, the fuel is often used in vain in practice. Therefore, the original method of preheating scrap by effectively utilizing the sensible heat of the exhaust gas from the electric furnace. There is a problem that it greatly contradicts the purpose.

<発明が解決しようとする問題点、その解決手段> 本発明は叙上の如き従来の問題点を解決する改良され
たスクラップ予熱後の排ガスの処理方法を提供するもの
である。
<Problems to be Solved by the Invention, Means for Solving the Problems> The present invention provides an improved method for treating exhaust gas after scrap preheating, which solves the above-mentioned conventional problems.

しかして本発明は、スクラップ予熱後の排ガスを燃料
を供給して燃焼させることにより脱臭し、脱臭後の排ガ
スを集塵装置を介して大気中へ放出する方法において、
スクラップ予熱後の排ガスを燃焼させるための燃料の供
給量をスクラップの性状及び/又はスクラップ予熱後の
排ガスの性状に応じて制御することを特徴とするスクラ
ップ予熱後の排ガスの処理方法に係る。
Thus, the present invention provides a method of deodorizing exhaust gas after scrap preheating by supplying fuel and burning it, and discharging the exhaust gas after deodorization to the atmosphere via a dust collector,
The present invention relates to a method for treating exhaust gas after preheating of scrap, characterized in that a supply amount of fuel for burning the exhaust gas after preheating of scrap is controlled according to the properties of the scrap and / or the properties of exhaust gas after preheating of scrap.

本発明では、スクラップ予熱後の排ガスを燃料を供給
して燃焼させることにより脱臭し、脱臭後の排ガスを集
塵装置で無害化した後に大気中へ放出するが、その肝要
な点は、スクラップの種類及びその組合わせによってほ
ぼ定量化される該スクラップ中の油分や塗料の比率に応
じ、及び/又はスクラップ予熱後の排ガス中の全炭化水
素濃度に応じて、スクラップ予熱後の排ガスを燃焼によ
り脱臭するために必要且つ充分な最低量の燃料を供給す
る処にある。
In the present invention, the exhaust gas after preheating of the scrap is deodorized by supplying and burning the fuel, and the exhaust gas after the deodorization is detoxified by the dust collecting device and then released to the atmosphere. Deodorizing by burning the exhaust gas after preheating the scrap according to the proportion of oil and paint in the scrap which is almost quantified by the type and combination thereof and / or according to the total hydrocarbon concentration in the exhaust gas after preheating the scrap To supply the minimum amount of fuel necessary and sufficient to

以下図面に基いて本発明の構成を更に詳細に説明す
る。第1図は本発明の一実施手順を略示する系統図であ
る。電気炉11からの排ガスが燃焼塔21で後燃焼され、バ
ルブ31,32で分岐された後、その一部又は全部がスクラ
ップ予熱装置41へと導入されて、スクラップ予熱装置41
で所定通りスクラップを予熱した後の排ガスが脱臭塔51
へと導入されている。そして、スクラップ予熱装置41と
脱臭塔51との間の系路には全炭化水素濃度検出用の検出
管61が枝管されており、検出管61を介して取り出された
スクラップ予熱後の排ガス中の全炭化水素濃度を全炭化
水素分析計62で分析し、全炭化水素分析計62の影響を受
けて演算装置63から発せられる信号により燃料供給系路
に組込まれた制御バルブ64の開度が調節され、脱臭塔51
への燃料供給量が制御されている。かくして、スクラッ
プ予熱後の排ガスを燃焼により脱臭するために必要且つ
充分な最低量の燃料供給によって、脱臭塔51で酸化分解
された後の排ガスは、バルブ31で分岐された排ガスと合
流し、吸引ファン71や更には図示しないクーラ等を経
て、集塵装置81で無害化されてから大気中へ放出されて
いる。
Hereinafter, the configuration of the present invention will be described in more detail with reference to the drawings. FIG. 1 is a system diagram schematically showing an operation procedure of the present invention. After the exhaust gas from the electric furnace 11 is post-combusted in the combustion tower 21 and branched at the valves 31 and 32, part or all of the exhaust gas is introduced into the scrap preheating device 41, and the scrap preheating device 41
The exhaust gas after preheating the scrap as specified in the deodorization tower 51
Has been introduced to. Further, a detection pipe 61 for detecting the total hydrocarbon concentration is branched in a system path between the scrap preheating device 41 and the deodorization tower 51, and the exhaust gas after the scrap preheating taken out through the detection pipe 61 is taken out through the detection pipe 61. Is analyzed by the total hydrocarbon analyzer 62, and the opening degree of the control valve 64 incorporated in the fuel supply line is determined by a signal issued from the arithmetic unit 63 under the influence of the total hydrocarbon analyzer 62. Regulated and deodorized tower 51
Is controlled. Thus, the exhaust gas after being oxidized and decomposed by the deodorization tower 51 is combined with the exhaust gas branched off by the valve 31 by the supply of a minimum amount of fuel necessary and sufficient to deodorize the exhaust gas after the scrap preheating by combustion, and is sucked. After being rendered harmless by a dust collector 81 via a fan 71 and a cooler (not shown) or the like, the dust is discharged to the atmosphere.

図面の場合、脱臭塔51への燃料供給量をスクラップ予
熱後の排ガス中の全炭化水素濃度に応じて制御している
が、かかる燃料供給量の制御は、スクラップ中の油分や
塗料の比率に応じて行なうこともできる。ダライ粉、シ
ュレッダ、Aプレス、Cプレス、甲山等、スクラップの
種類によって該スクラップ中に含まれる油分や塗料の比
率はほぼ一定であるので、予熱するスクラップの種類と
その組合わせ(使用割合)によって該スクラップ中に含
まれる油分や塗料の比率もほぼ定量化される。一方、か
かる油分や塗料に起因して発生するところのスクラップ
予熱後の排ガス中の悪臭成分を燃焼により酸化分解する
ために必要且つ充分な最低量の燃料は予測することがで
きるので、該予測を活用して、スクラップ中の油分や塗
料の比率に応じ燃料供給量を制御するのである。このよ
うなスクラップの性状に応じた制御と前述したようなス
クラップ予熱後の排ガス中の全炭化水素濃度に応じた制
御とを併用すれば、より好ましく合目的的にスクラップ
予熱後の排ガスを脱臭することができる。
In the case of the drawing, the fuel supply amount to the deodorization tower 51 is controlled according to the total hydrocarbon concentration in the exhaust gas after the scrap preheating, but the control of the fuel supply amount depends on the ratio of oil and paint in the scrap. It can be done accordingly. Depending on the type of scrap, such as Dalai powder, shredder, A-press, C-press, Kayama, etc., the ratio of oil and paint contained in the scrap is almost constant, so depending on the type of preheated scrap and its combination (use ratio) The ratio of oil and paint contained in the scrap is also almost quantified. On the other hand, a minimum and sufficient amount of fuel necessary and sufficient to oxidatively decompose the odorous components in the exhaust gas after the preheating of the scrap generated by the oil and the paint by combustion can be predicted. Utilizing it, the fuel supply is controlled according to the ratio of oil and paint in the scrap. If the control according to the properties of the scrap and the control according to the total hydrocarbon concentration in the exhaust gas after the preheating of the scrap as described above are used together, the exhaust gas after the preheating of the scrap is more preferably and purposefully deodorized. be able to.

<実施例> 前述した第1図の系統図に準じて、混合スクラップを
予熱し、予熱後の排ガスを脱臭した後、集塵装置を介し
て大気中へ放出した。下記実施例1及び2は、混合スク
ラップの性状に応じて脱臭塔への燃料供給量を制御した
場合であり、また下記実施例3は混合スクラップ予熱後
の排ガス中の全炭化水素濃度に応じて脱臭塔への燃料供
給量を制御した場合である。
<Example> According to the system diagram of Fig. 1 described above, the mixed scrap was preheated, and the exhaust gas after preheating was deodorized, and then discharged to the atmosphere via a dust collector. The following Examples 1 and 2 are cases in which the amount of fuel supplied to the deodorization tower was controlled according to the properties of the mixed scrap, and Example 3 below was determined according to the total hydrocarbon concentration in the exhaust gas after preheating the mixed scrap. This is a case where the fuel supply amount to the deodorization tower is controlled.

・実施例1:ダライ粉10000Kg(油分2重量%、塗料0重
量%)、シュレッダ20000Kg(油分0.5重量%、塗料1重
量%)、及びCプレス10000Kg(油分1重量%、塗料2
重量%)の混合スクラップを予熱した。燃料供給量を15
0/時に制御した結果、脱臭塔からの排ガス中に悪臭
は全く認められなかった(官能検査とガスクロマトグラ
フ分析、以下同じ)。
Example 1: 10,000 kg of Dalai powder (2% by weight of oil, 0% by weight of paint), 20,000 kg of shredder (0.5% by weight of oil, 1% by weight of paint), and 10,000 kg of C press (1% by weight of oil, 2% of paint)
Wt%) of the mixed scrap was preheated. 15 fuel supply
As a result of controlling at 0 / h, no odor was found in the exhaust gas from the deodorization tower (sensory test and gas chromatographic analysis, the same applies hereinafter).

・実施例2:実施例1と同じ原料を使用し、ダライ粉5000
Kg、シュレッダ10000Kg、及びCプレス10000Kgの混合ス
クラップを予熱した。燃料供給量を115/時に制御し
た結果、脱臭塔からの排ガス中に悪臭は全く認められな
かった。
Example 2: Using the same raw material as in Example 1, Dalai powder 5000
A mixed scrap of Kg, 10,000 kg of shredder and 10,000 kg of C-press was preheated. As a result of controlling the fuel supply amount to 115 / hour, no odor was found in the exhaust gas from the deodorization tower.

・実施例3:予熱後の排ガス中の全炭化水素濃度が30ppm
の混合スクラップを予熱した。燃料供給量を65/時に
制御した結果、脱臭塔からの排ガス中に悪臭は全く認め
られかった。
Example 3: The total hydrocarbon concentration in the exhaust gas after preheating is 30 ppm
Was preheated. As a result of controlling the fuel supply rate to 65 / h, no odor was found in the exhaust gas from the deodorization tower.

<発明の効果> 以上説明した通りであるから、本発明には、スクラッ
プ予熱後の排ガスを最も省エネルギ化された条件下で脱
臭して処理することができるという効果がある。
<Effect of the Invention> As described above, the present invention has an effect that the exhaust gas after the preheating of the scrap can be deodorized and treated under the most energy-saving condition.

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

第1図は本発明の一実施手順を略示する系統図である。 11……電気炉、21……燃焼塔 31,32……バルブ 41……スクラップ予熱装置、51……脱臭塔 62……全炭化水素分析計、63……演算装置 64……制御バルブ、81……集塵装置 FIG. 1 is a system diagram schematically showing an operation procedure of the present invention. 11: Electric furnace, 21: Combustion tower 31, 32: Valve 41: Scrap preheating device, 51: Deodorizing tower 62: Total hydrocarbon analyzer, 63: Calculation device 64: Control valve, 81 …… Dust collector

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】スクラップ予熱後の排ガスを燃料を供給し
て燃焼させることにより脱臭し、脱臭後の排ガスを集塵
装置を介して大気中へ放出する方法において、スクラッ
プ予熱後の排ガスを燃焼させるための燃料の供給量をス
クラップの性状及び/又はスクラップ予熱後の排ガスの
性状に応じて制御することを特徴とするスクラップ予熱
後の排ガスの処理方法。
1. A method for deodorizing exhaust gas after scrap preheating by supplying fuel and burning the exhaust gas, and discharging the exhaust gas after deodorization to the atmosphere via a dust collector, the exhaust gas after scrap preheating is burned. A method for treating the exhaust gas after the preheating of the scrap, characterized in that the supply amount of the fuel is controlled according to the properties of the scrap and / or the properties of the exhaust gas after the preheating of the scrap.
【請求項2】燃料の供給量をスクラップ中の油分及び塗
料の比率に応じて制御する特許請求の範囲第1項記載の
スクラップ予熱後の排ガスの処理方法。
2. The method for treating exhaust gas after preheating of scrap according to claim 1, wherein the supply amount of fuel is controlled according to the ratio of oil and paint in the scrap.
【請求項3】燃料の供給量をスクラップ予熱後の排ガス
中の全炭化水素濃度に応じて制御する特許請求の範囲第
1項記載のスクラップ予熱後の排ガスの処理方法。
3. The method for treating exhaust gas after preheating of scrap according to claim 1, wherein the supply amount of fuel is controlled according to the total hydrocarbon concentration in the exhaust gas after preheating of scrap.
JP31438387A 1987-12-11 1987-12-11 Exhaust gas treatment method after scrap preheating Expired - Lifetime JP2595590B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP31438387A JP2595590B2 (en) 1987-12-11 1987-12-11 Exhaust gas treatment method after scrap preheating

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP31438387A JP2595590B2 (en) 1987-12-11 1987-12-11 Exhaust gas treatment method after scrap preheating

Publications (2)

Publication Number Publication Date
JPH01155195A JPH01155195A (en) 1989-06-19
JP2595590B2 true JP2595590B2 (en) 1997-04-02

Family

ID=18052680

Family Applications (1)

Application Number Title Priority Date Filing Date
JP31438387A Expired - Lifetime JP2595590B2 (en) 1987-12-11 1987-12-11 Exhaust gas treatment method after scrap preheating

Country Status (1)

Country Link
JP (1) JP2595590B2 (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6346384A (en) * 1986-08-14 1988-02-27 石川島播磨重工業株式会社 Scrap preheating method by furnace exhaust gas

Also Published As

Publication number Publication date
JPH01155195A (en) 1989-06-19

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