JPH11190594A - Method and device for treating exhaust gas of electric furnace for steel manufacture - Google Patents

Method and device for treating exhaust gas of electric furnace for steel manufacture

Info

Publication number
JPH11190594A
JPH11190594A JP9358452A JP35845297A JPH11190594A JP H11190594 A JPH11190594 A JP H11190594A JP 9358452 A JP9358452 A JP 9358452A JP 35845297 A JP35845297 A JP 35845297A JP H11190594 A JPH11190594 A JP H11190594A
Authority
JP
Japan
Prior art keywords
exhaust gas
temperature
electric furnace
duct
combustion chamber
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
JP9358452A
Other languages
Japanese (ja)
Inventor
Takahiro Hosokawa
隆弘 細川
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.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan 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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP9358452A priority Critical patent/JPH11190594A/en
Publication of JPH11190594A publication Critical patent/JPH11190594A/en
Pending 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

Abstract

PROBLEM TO BE SOLVED: To prevent dioxins in dust being gathered inside a duct or the like when a high-temperature exhaust gas flows from being scattered again after a low- temperature exhaust gas flows. SOLUTION: Two groups of systems for treating a high-temperature gas being generated from an electric furnace 1 for steel manufacture are provided. When the temperature of the exhaust gas is equal to or more than a fixed value being predetermined based on the combustion decomposition temperature of dioxin, the exhaust gas is cooled by a cooling device 10 and is purified and treated by a dust collector 12. When the temperature of the exhaust gas is less than the fixed value, the exhaust gas is led to and is cooled by another cooling device 10' and is purified and treated by a dust collector 12' at the downstream of the cooling device 10'. In this case, the fixed temperature is 800 deg.C, thus satisfying the target value (for example, 0.5 ng-TEQ/ Nm<3> or less) of the concentration of dioxins in the exhaust gas being dissipated into air, at the same time, reducing the absolute value of exhaustion and the amount of the treatment of the dust containing dioxins, and, furthermore, eliminating the need for secondary burning facilities as in a conventional combustion decomposition method and the running costs.

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】この発明は、鉄スクラップ等
を溶解・精錬して鉄鋼を製造するための製鋼用電気炉設
備の操業中に、電気炉から発生する排ガスを冷却し清浄
化処理する技術であって、特にこの排ガス中に含まれる
ダイオキシン等の有毒物質の発生を抑制し、除去する方
法及びそのような装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a technology for cooling and purifying exhaust gas generated from an electric furnace during the operation of a steelmaking electric furnace facility for producing steel by melting and refining iron scrap and the like. In particular, the present invention relates to a method for suppressing and removing toxic substances such as dioxins contained in the exhaust gas, and to a device for such a method.

【0002】[0002]

【従来の技術】製鋼用電気炉では、通常、鉄スクラップ
を主原料としてアークエネルギー又は高周波エネルギー
等により加熱溶解し、酸化精錬及び還元精錬を行ない、
溶湯を取鍋に出鋼し、その際合金鉄を添加して溶湯の成
分を調整して溶鋼を製造する。このように、製鋼用電気
炉で鉄スクラップを加熱溶解し、得られた溶湯を精錬
し、取鍋に出鋼し、そしてスラグを排滓する一連の工程
において、電気炉からは排ガスが発生する。この排ガス
中には、CO、CO2 、N2 、O2 、H2 及びH2O等
のガス成分、酸化鉄微粉、及び、ZnやSnのような高
蒸気圧金属元素の他に、有毒物質であるダイオキシンが
含まれている。ダイオキシンの発生源は、溶解主原料の
鉄スクラップに付着・混入している塩化ビニールやプラ
スティック塗料等に起因する有機塩素系化合物にあり、
これらが所定の条件下で燃焼する場合に生成する。電気
炉から発生する排ガスは、所定の装置で冷却され、集塵
機に導かれ、ダストが除去され、清浄化処理が施され、
その結果、排ガス中の粉塵含有率及び有害物質成分濃度
等が規定値以下になった後に大気へ放散される。従っ
て、製鋼用電気炉の操業においては、ダイオキシンが生
成しないような条件下で操業することが望まれている。
2. Description of the Related Art In an electric furnace for steelmaking, usually, iron scrap is mainly heated and melted by arc energy or high-frequency energy to perform oxidation refining and reduction refining.
The molten metal is tapped into a ladle, and alloy iron is added to adjust the components of the molten metal to produce molten steel. Thus, in a series of steps of heating and melting iron scrap in a steelmaking electric furnace, refining the resulting molten metal, tapping into a ladle, and discharging the slag, exhaust gas is generated from the electric furnace. . This exhaust gas contains toxic components other than gas components such as CO, CO 2 , N 2 , O 2 , H 2 and H 2 O, iron oxide fine powder, and high vapor pressure metal elements such as Zn and Sn. Contains the substance dioxin. The source of dioxin is organic chlorine-based compounds caused by vinyl chloride, plastic paint, etc. attached to and mixed with iron scrap as the main raw material for dissolution.
They are formed when they burn under predetermined conditions. Exhaust gas generated from the electric furnace is cooled by a predetermined device, guided to a dust collector, dust is removed, a cleaning process is performed,
As a result, after the dust content rate and the concentration of harmful substance components in the exhaust gas have fallen below the specified values, they are released to the atmosphere. Therefore, in the operation of an electric furnace for steelmaking, it is desired to operate under conditions that do not generate dioxin.

【0003】図3に、従来の製鋼用電気炉の排ガス処理
装置例の概略フロー図を示す。同図において、1は製鋼
用電気炉、2は燃焼室、2’は二次燃焼装置、9は散水
式スプレー冷却塔、12は集塵機である。電気炉1から
発生した高温の排ガス1aを燃焼室2に導き、排ガス中
の可燃ガスを燃焼させると共に、更に二次燃焼装置2’
であるバーナー等で排ガスを加熱して、その排ガス温度
を高め、排ガス中のダイオキシンを燃焼分解させる。次
いで、ダイオキシンの無くなった排ガスを水冷ダクト3
に通して間接冷却し、そして、散水式スプレー冷却塔9
に導き直接冷却する。
FIG. 3 shows a schematic flow chart of an example of a conventional exhaust gas treatment apparatus for an electric furnace for steelmaking. In the figure, 1 is an electric furnace for steelmaking, 2 is a combustion chamber, 2 'is a secondary combustion device, 9 is a spray spray cooling tower, and 12 is a dust collector. The high-temperature exhaust gas 1a generated from the electric furnace 1 is led to the combustion chamber 2, where the combustible gas in the exhaust gas is burned and the secondary combustion device 2 'is further burned.
The exhaust gas is heated by a burner or the like, the temperature of the exhaust gas is raised, and dioxin in the exhaust gas is burned and decomposed. Next, the exhaust gas from which dioxin has been removed is passed through a water-cooled duct 3
Indirect cooling through a water spray spray tower 9
And cooled directly.

【0004】この排ガス冷却では、ダイオキシンの再合
成反応を阻止するために、排ガス温度を350℃以上か
ら250℃以下まで急冷する。この急冷が不十分な場合
はダイオキシンの再合成により排ガスは汚れる。集塵機
12としてのバグフィルター入口での排ガス温度を望ま
しくは80℃以下まで下げて、排ガス中の粉塵にダイオ
キシンを吸着させ、ダイオキシンが吸着した粉塵をバグ
フィルターで捕集する。こうして、ダイオキシン及び粉
塵が除去された排ガス14aを煙突14から放散する
(以下、「先行技術」という)。
In this exhaust gas cooling, the temperature of the exhaust gas is rapidly cooled from 350 ° C. or higher to 250 ° C. or lower in order to prevent the resynthesis reaction of dioxin. If the quenching is insufficient, the exhaust gas is contaminated by the resynthesis of dioxin. The temperature of the exhaust gas at the inlet of the bag filter as the dust collector 12 is desirably lowered to 80 ° C. or less, so that dioxin is adsorbed on dust in the exhaust gas, and the dust adsorbed by dioxin is collected by the bag filter. Thus, the exhaust gas 14a from which dioxins and dust have been removed is emitted from the chimney 14 (hereinafter referred to as "prior art").

【0005】[0005]

【発明が解決しようとする課題】上述した先行技術に
は、下記問題点がある。先行技術は、電気炉から発生す
る排ガス中にダイオキシンが含まれているときでも、燃
焼室における二次燃焼装置の運転条件を管理し、燃焼室
内温度を所定値以上の高温に維持する。こうして、ダイ
オキシンを燃焼室内で燃焼分解させ、燃焼室から排出さ
れる排ガス中のダイオキシンを無くし、更に、このダイ
オキシンの含まれない排ガスを冷却する。この冷却過程
の内、ダイオキシンの低温における再合成を抑止するた
めに、350℃以上から250℃以下までこの排ガスを
急冷する。
The above prior art has the following problems. The prior art manages the operating conditions of the secondary combustion device in the combustion chamber even when the exhaust gas generated from the electric furnace contains dioxin, and maintains the temperature of the combustion chamber at a high temperature equal to or higher than a predetermined value. In this way, dioxin is burned and decomposed in the combustion chamber, dioxin in exhaust gas discharged from the combustion chamber is eliminated, and the exhaust gas not containing dioxin is cooled. During the cooling process, the exhaust gas is rapidly cooled from 350 ° C. or higher to 250 ° C. or lower in order to suppress the resynthesis of dioxin at a low temperature.

【0006】しかしながら、電気炉から発生する排ガス
の温度が相当に低いとき、例えば、電気炉操業において
連続稼働が中断した後の最初のヒート等においては、1
ヒートサイクル中でも原料初装入時期や追加装入時期の
ようなときには、二次燃焼装置による燃焼室内での熱量
付加のみで燃焼室出口温度を800℃以上に維持するた
めには、過大な能力の二次燃焼装置が必要となる。そし
て、電気炉からの排ガス温度が低い時期には、燃焼室出
口での排ガス温度が800℃以下になることがある。こ
のような場合には、排ガス中にはダイオキシンが存在し
たままの排ガスが排ガス流路を流れることになる。そし
て途中のダクト内部等に溜まった粉塵にはダイオキシン
が吸着されて含まれることになる。
[0006] However, when the temperature of the exhaust gas generated from the electric furnace is considerably low, for example, in the first heat after the continuous operation is interrupted in the operation of the electric furnace or the like, 1
During the heat cycle, such as during the initial charging of raw materials or during the additional charging, in order to maintain the temperature of the combustion chamber outlet at 800 ° C or higher only by adding heat in the combustion chamber by the secondary combustion device, excessive capacity is required. A secondary combustion device is required. When the temperature of the exhaust gas from the electric furnace is low, the temperature of the exhaust gas at the outlet of the combustion chamber may be 800 ° C. or less. In such a case, the exhaust gas containing dioxin in the exhaust gas flows through the exhaust gas channel. Then, dioxin is adsorbed and contained in the dust accumulated in the duct and the like on the way.

【0007】このように、電気炉からの排ガス温度が低
い時期には、ダイオキシンが吸着した粉塵がダクト等に
溜まり易い。ところが、その後において、高温度の排ガ
スがダクト等を流れると、上記粉塵中のダイオキシンは
粉塵から離脱して排ガスと共に再飛散する。再飛散した
ダイオキシンは粉塵から離れ、ガス中に混入して飛散す
るに至る。
As described above, when the temperature of the exhaust gas from the electric furnace is low, dust adsorbed by dioxin tends to accumulate in ducts and the like. However, after that, when high-temperature exhaust gas flows through a duct or the like, dioxin in the dust separates from the dust and re-scatters together with the exhaust gas. The re-scattered dioxin separates from the dust and enters the gas and scatters.

【0008】従って、この発明の課題は、比較的低温の
排ガスが流れた後でダクト内部等に溜まった粉塵中に含
まれているダイオキシンが、その後において比較的高温
の排ガスが流れたときに、上記溜まった粉塵からダイオ
キシンが再飛散するような現象を防止する。そして、バ
グフィルター等の集塵装置に溜まったダイオキシンを含
む粉塵の処理を効率的に行なうことができるようにする
ことにある。
Accordingly, an object of the present invention is to solve the problem that dioxin contained in dust accumulated in a duct or the like after a relatively low temperature exhaust gas has flowed and a relatively high temperature exhaust gas subsequently flows. The phenomenon that dioxin re-scatters from the accumulated dust is prevented. It is another object of the present invention to efficiently treat dust containing dioxin accumulated in a dust collector such as a bag filter.

【0009】[0009]

【課題を解決するための手段】上述した観点から、製鋼
用電気炉の排ガス処理方法を開発すべく鋭意研究を重ね
た。本発明者等は、製鋼用電気炉から発生する排ガス中
のダイオキシン濃度は、排ガスの温度と強い相関があ
り、ダイオキシン濃度は溶解初期等の排ガス温度が低い
時期においては非常に高いが、その温度が800℃を超
えると極めて低くなるという知見を得た。そこで、電気
炉から発生した排ガスが燃焼室で燃焼した後の温度が、
ダイオキシンが燃焼分解する温度以上の場合とそれ未満
の場合とに区別し、燃焼室から排出された排ガスの処理
系統を高低に2分し、高低別にこの処理系統を専用にす
ることを着想した。この発明は上記知見と着想に基づき
なされたものである。
SUMMARY OF THE INVENTION In view of the above, intensive studies have been made to develop an exhaust gas treatment method for an electric furnace for steelmaking. The present inventors have found that the concentration of dioxin in exhaust gas generated from an electric furnace for steelmaking has a strong correlation with the temperature of exhaust gas, and the concentration of dioxin is very high at the time of low exhaust gas temperature such as in the initial stage of dissolution. Is extremely low when the temperature exceeds 800 ° C. Therefore, the temperature after the exhaust gas generated from the electric furnace burns in the combustion chamber,
The case where the temperature is equal to or higher than the temperature at which dioxin is decomposed by combustion is distinguished from the case where the temperature is lower than the temperature. The present invention has been made based on the above findings and ideas.

【0010】請求項1記載の製鋼用電気炉の排ガス処理
方法は、製鋼用電気炉の操業過程で電気炉から発生する
高温の排ガスを燃焼室及び/又はダクトに導き、その排
ガス中の未燃ガス成分を燃焼室及び/又はダクトで燃焼
させ、この燃焼室及び/又はダクトから排出された高温
の排ガスを、冷却装置で冷却し、次いで集塵装置に導
き、この排ガスを集塵装置で浄化処理する製鋼用電気炉
の排ガス処理方法において、次のとおり排ガスの冷却工
程を大きく2系列に分けて処理することに特徴を有する
ものである。
According to a first aspect of the present invention, there is provided a method for treating exhaust gas from an electric furnace for steelmaking, wherein high-temperature exhaust gas generated from the electric furnace during the operation of the electric furnace for steelmaking is led to a combustion chamber and / or a duct, and unburned exhaust gas in the exhaust gas. Gas components are burned in a combustion chamber and / or a duct, and high-temperature exhaust gas discharged from the combustion chamber and / or a duct is cooled by a cooling device, and then guided to a dust collector, and the exhaust gas is purified by the dust collector. An exhaust gas treatment method for a steelmaking electric furnace to be treated is characterized in that an exhaust gas cooling process is divided into two main processes as follows.

【0011】燃焼室及び/又はダクトから排出される
排ガスの温度がダイオキシンの燃焼分解温度を考慮して
予め定めた一定値以上のときには、燃焼室及び/又はダ
クトから排出された排ガスを、冷却装置に導きこの冷却
装置で冷却し、次いで上記冷却装置の下流に配設された
集塵装置にこの排ガスを導き、この集塵装置で浄化処理
する。
When the temperature of the exhaust gas discharged from the combustion chamber and / or the duct is equal to or higher than a predetermined value in consideration of the combustion decomposition temperature of dioxin, the exhaust gas discharged from the combustion chamber and / or the duct is cooled. Then, the exhaust gas is guided to a dust collecting device disposed downstream of the cooling device, and is purified by the dust collecting device.

【0012】これに対して、燃焼室及び/又はダクト
から排出される排ガスの温度が、上記一定値未満のとき
には、燃焼室及び/又はダクトから排出された排ガス
を、上記冷却装置を除く他の冷却装置に導き、この冷却
装置で冷却し、次いでこの冷却装置の下流に配設された
集塵装置にこの排ガスを導き、この集塵装置で浄化処理
する。
On the other hand, when the temperature of the exhaust gas discharged from the combustion chamber and / or the duct is lower than the above-mentioned fixed value, the exhaust gas discharged from the combustion chamber and / or the duct is discharged to another unit except the cooling device. The exhaust gas is guided to a cooling device, cooled by the cooling device, and then guided to a dust collecting device disposed downstream of the cooling device, and the exhaust gas is purified by the dust collecting device.

【0013】請求項2記載の製鋼用電気炉の排ガス処理
装置は、次の装置及び機構を備えたものであることに特
徴を有するものである。即ち、製鋼用電気炉と、この電
気炉から発生する排ガス中の未燃ガス成分を燃焼させる
燃焼室及び/又はダクトと、この燃焼室及び/又はダク
トから排出される排ガス温度を測定し、この温度情報に
基づき燃焼室及び/又はダクトから排出された排ガスを
次工程へ導くべき排ガス流路を複数の排ガス流路の中か
ら選定をし、この選定結果に基づき上記排ガスを上記選
定された排ガス流路に導くための排ガス流路切替え機構
と、上記複数の排ガス流路の各々に通じて配設された排
ガスの冷却装置及びこの冷却装置の下流側に通じて配設
された集塵装置からなる、複数の冷却・集塵装置系とを
備えたものである。
An exhaust gas treatment apparatus for a steelmaking electric furnace according to a second aspect of the present invention is characterized by having the following apparatus and mechanism. That is, a steelmaking electric furnace, a combustion chamber and / or a duct for burning unburned gas components in exhaust gas generated from the electric furnace, and an exhaust gas temperature discharged from the combustion chamber and / or the duct were measured. Based on the temperature information, an exhaust gas path from which the exhaust gas discharged from the combustion chamber and / or the duct is to be led to the next process is selected from a plurality of exhaust gas paths, and the exhaust gas is selected based on the selection result. An exhaust gas passage switching mechanism for guiding the exhaust gas to a flow passage, a cooling device for the exhaust gas arranged to communicate with each of the plurality of exhaust gas passages, and a dust collecting device arranged to a downstream side of the cooling device. And a plurality of cooling / dust collecting device systems.

【0014】請求項3記載の製鋼用電気炉の排ガス処理
方法は、請求項2に記載した排ガス処理装置における複
数の排ガス流路と複数の冷却・集塵装置系との組合せか
らなる系の数が2つである製鋼用電気炉の排ガス処理装
置を用い、請求項1に記載した排ガス処理方法における
ダイオキシンの燃焼分解温度に基づき予め定めた一定値
として800℃を採用し、燃焼室及び/又はダクトから
排出される排ガス温度が800℃以上である場合には常
に一方の前記排ガス流路に導き、上記一定値の温度が8
00℃未満である場合には常にもう一方の排ガス流路に
導くことに特徴を有するものである。
According to a third aspect of the present invention, there is provided an exhaust gas treating method for a steelmaking electric furnace, wherein the number of systems comprising a combination of a plurality of exhaust gas passages and a plurality of cooling / dust collecting systems in the exhaust gas treating apparatus according to the second aspect. Using an exhaust gas treatment device of an electric furnace for steelmaking, wherein 800 ° C. is adopted as a predetermined value based on the combustion decomposition temperature of dioxin in the exhaust gas treatment method according to claim 1, and the combustion chamber and / or When the temperature of the exhaust gas discharged from the duct is 800 ° C. or higher, the exhaust gas is always led to one of the exhaust gas channels, and the temperature of the constant value is set to 8
When the temperature is lower than 00 ° C., it is always guided to the other exhaust gas flow path.

【0015】[0015]

【発明の実施の形態】次に、この発明を、図面を参照し
ながら説明する。図1は、この発明の電気炉の排ガス処
理方法を実施するための排ガス処理装置例を示す概略フ
ロー図である。この装置は、電気炉1、燃焼室2、排ガ
ス流路切替え装置5、冷却装置10、10’、集塵装置
12、12’、及び、これらの各装置間で排ガスを輸送
・冷却・燃焼を適宜実施するダクト群からなる。この発
明の排ガス処理装置の最大の特徴は、このように冷却装
置及び集塵装置からなる冷却・集塵装置系が2系列設け
られていることである。
Next, the present invention will be described with reference to the drawings. FIG. 1 is a schematic flow chart showing an example of an exhaust gas treatment apparatus for carrying out the method for treating exhaust gas of an electric furnace according to the present invention. This device includes an electric furnace 1, a combustion chamber 2, an exhaust gas flow switching device 5, cooling devices 10, 10 ', dust collecting devices 12, 12', and transport, cooling, and combustion of exhaust gas among these devices. It consists of a group of ducts that are implemented as appropriate. The most significant feature of the exhaust gas treatment device of the present invention is that two cooling / dust collection systems including the cooling device and the dust collection device are provided.

【0016】電気炉1から発生した高温の排ガス1aは
エルボー管1b及び摺動管1cを通って集煙管1dに吸
い込まれ、次いで排ガス1eとなり、燃焼室2に入る。
摺動管1cは、エルボー管1bと集煙管1dとの間にあ
って高温の排ガス1aを集煙管1dに吸引する際に、排
ガス1aと共に外気を吸い込ませるために集煙管1d軸
心方向に摺動して導管に適当な隙間を形成させる機能を
もつ。こうして外気の空気を含んだ排ガス1eは、燃焼
室2内で排ガス1e中の未燃ガス成分、例えばCOやH
2 が燃焼し、その結果排ガス1eの温度は上昇する。そ
して、燃焼室2の出側に設置された排ガス温度指示制御
装置4が、排ガス4aの温度を測定すると共に、その測
定値を排ガス流量調整器5a、5bに電送し、排ガス4
aを流路Aに流すか、流路Bに流すかを指示する。上記
一定温度の値として、例えば、800℃を採用する。
The high-temperature exhaust gas 1a generated from the electric furnace 1 passes through the elbow pipe 1b and the sliding pipe 1c, is sucked into the smoke collection pipe 1d, then becomes the exhaust gas 1e, and enters the combustion chamber 2.
The sliding pipe 1c is located between the elbow pipe 1b and the smoke collecting pipe 1d, and slides in the axial direction of the smoke collecting pipe 1d to suck outside air together with the exhaust gas 1a when the high temperature exhaust gas 1a is sucked into the smoke collecting pipe 1d. To form an appropriate gap in the conduit. In this way, the exhaust gas 1e containing the outside air becomes uncombusted gas components in the exhaust gas 1e in the combustion chamber 2, for example, CO or H
2 is burned, resulting temperature of the exhaust gas 1e is increased. Then, the exhaust gas temperature instruction control device 4 installed on the outlet side of the combustion chamber 2 measures the temperature of the exhaust gas 4a, and transmits the measured value to the exhaust gas flow rate regulators 5a and 5b.
a to flow through the flow path A or flow path B. As the value of the constant temperature, for example, 800 ° C. is adopted.

【0017】排ガス温度指示制御装置4は、 排ガス4aの温度が800℃以上のときは、排ガス流
量調整器5aに対して開の指示、排ガス流量調整器5b
に対して閉の指示を出す。排ガス4aは流路Aに流れ、
冷却装置10、及び集塵装置12の冷却・集塵系が機能
する。 また、排ガス4aの温度が800℃未満のときは、排
ガス流量調整器5bに対して開の指示、排ガス流量調整
器5aに対して閉の指示を出す。排ガス4aは流Bに流
れ、冷却装置10’、及び集塵装置12’の冷却・集塵
系が機能する。
When the temperature of the exhaust gas 4a is 800 ° C. or higher, the exhaust gas temperature instruction controller 4 instructs the exhaust gas flow controller 5a to open, and the exhaust gas flow controller 5b
Instruct to close. The exhaust gas 4a flows to the channel A,
The cooling / dust collection system of the cooling device 10 and the dust collection device 12 functions. When the temperature of the exhaust gas 4a is lower than 800 ° C., an instruction to open the exhaust gas flow controller 5b and an instruction to close the exhaust gas flow controller 5a are issued. The exhaust gas 4a flows to the stream B, and the cooling / dust collecting system of the cooling device 10 'and the dust collecting device 12' functions.

【0018】上記の排ガス4a温度が高いときは、ダ
イオキシンは燃焼分解しているが、の排ガス4a温度
が低いときは、ダイオキシンは燃焼分解するに至らず、
これが含まれている。
When the temperature of the exhaust gas 4a is high, dioxin is decomposed by combustion, but when the temperature of the exhaust gas 4a is low, dioxin is not decomposed by combustion.
This is included.

【0019】排ガス4a温度が高いのときは、排ガス
4aを次工程の水冷ダクト3で400℃前後まで冷却
し、次いで、水スプレー冷却塔9で、350℃以上から
250℃以下まで急冷する。この急冷によりダイオキシ
ンは再合成されず、また、元々ダイオキシンは含まれて
いない。従って、少なくともバグフィルターの耐熱温度
である200℃程度で集塵装置12に導いてもよい。バ
グフィルターで粉塵を除去し、浄化された排ガス14a
を煙突14から放散する。この場合は、粉塵中にダイオ
キシンは殆ど含まれない。
When the temperature of the exhaust gas 4a is high, the exhaust gas 4a is cooled to about 400 ° C. in the next step of the water cooling duct 3, and then rapidly cooled in the water spray cooling tower 9 from 350 ° C. or higher to 250 ° C. or lower. Dioxin is not resynthesized by this quenching, and dioxin is not originally contained. Therefore, it may be guided to the dust collecting device 12 at least at about 200 ° C. which is the heat-resistant temperature of the bag filter. Exhaust gas 14a purified by removing dust with a bag filter
From the chimney 14. In this case, the dust contains almost no dioxin.

【0020】これに対して、排ガス4a温度が低いの
ときは、排ガス4aを次工程の水冷ダクト3’で400
℃前後まで冷却し、次いで、水スプレー冷却塔9’で、
350℃以上から250℃以下まで急冷する。この急冷
によりダイオキシンは新たな再合成はされないが、元々
排ガス4a中にはダイオキシンが含まれている。従っ
て、排ガスを80℃程度以下まで冷却し、ダイオキシン
を粉塵に吸着させた後に集塵装置12’のバグフィルタ
ーで処理する。この場合はバグフィルターで捕捉された
粉塵中には、ダイオキシンが含まれている。
On the other hand, when the temperature of the exhaust gas 4a is low, the exhaust gas 4a is
° C, and then in a water spray cooling tower 9 '
Rapid cooling from 350 ° C or higher to 250 ° C or lower. Dioxin is not newly resynthesized by this quenching, but dioxin is originally contained in the exhaust gas 4a. Therefore, the exhaust gas is cooled to about 80 ° C. or less, and the dioxin is adsorbed on the dust, and then treated with the bag filter of the dust collector 12 ′. In this case, the dust captured by the bag filter contains dioxin.

【0021】この発明では、上述したように、燃焼室2
を出た後の排ガス4a中にダイオキシンが含まれている
場合と、含まれていない場合とで、以後の冷却・集塵処
理系を専用的に分けたので、この発明の目的とするダイ
オキシン含有粉塵からのダイオキシンの再飛来を防止す
ることができる。
In the present invention, as described above, the combustion chamber 2
The following cooling / dust collection system is dedicated to the case where the dioxin is contained in the exhaust gas 4a after leaving the exhaust gas, and the case where the dioxin is not contained. It is possible to prevent dioxin from coming back from dust.

【0022】なお、上記の場合には、活性炭や水酸化
カルシウム等の吸着剤吹込み装置16を冷却装置10の
下流側であって集塵装置12の上流側のダクトの途中に
設置し、吸着剤を吹込み、排ガス中に含まれるダイオキ
シンを吸着させ、しかる後に集塵装置12’で処理する
のが一層望ましい。また、の場合も同様にすれば更に
清浄な排ガス14aが得られる。
In the above case, the adsorbent blowing device 16 such as activated carbon or calcium hydroxide is installed on the downstream side of the cooling device 10 and in the middle of the duct on the upstream side of the dust collecting device 12 so as to adsorb the adsorbent. It is more desirable to inject the agent to adsorb the dioxin contained in the exhaust gas, and then treat the dioxin in the dust collector 12 '. Also, in the case of the above, a further clean exhaust gas 14a can be obtained.

【0023】図2に、この発明の電気炉の排ガス処理方
法を実施するための排ガス処理装置の他の例の概略フロ
ー図を示す。この装置は、図1の装置との相違点は、排
ガスの冷却装置として、はじめに水スプレー冷却塔を配
置し、次いで大量の建屋集塵ガスで急冷する構成とした
ことである。その他の装置構成は、図1の場合と同じで
ある。
FIG. 2 shows a schematic flow chart of another example of an exhaust gas treatment apparatus for carrying out the method for treating exhaust gas of an electric furnace according to the present invention. This apparatus is different from the apparatus shown in FIG. 1 in that a water spray cooling tower is first disposed as a cooling apparatus for exhaust gas, and then a rapid cooling is performed with a large amount of building dust gas. Other device configurations are the same as those in FIG.

【0024】次に、表1に、従来法による燃焼室後の排
ガス4a処理系を、その排ガス温度により分けない場合
と、本発明の排ガス温度が800℃を境界として燃焼室
後の排ガス4a処理系を専用系にして分けた場合につい
て、ダイオキシンの挙動を調査した。表1に、その一例
を示す。
Next, Table 1 shows that the conventional exhaust gas 4a treatment system after the combustion chamber is not divided according to the exhaust gas temperature, and that the present invention treats the exhaust gas 4a after the combustion chamber at 800 ° C. as a boundary. The behavior of dioxin was investigated when the system was divided into dedicated systems. Table 1 shows an example.

【0025】[0025]

【表1】 [Table 1]

【0026】[0026]

【発明の効果】以上述べたように、この発明によれば、
製鋼用電気炉の操業過程で電気炉から発生するガス中に
含まれるダイオキシンの発生を抑止するに当たり、冷却
・集塵処理系を、排ガス中にダイオキシンが含まれる場
合(低温排ガス)と含まれない場合(高温排ガス)とで
分けたので、高温排ガスを処理したときに低温排ガス処
理によりダクト等に溜まった粉塵からのダイオキシンの
再飛来がなくなる。従って、大気中への放散排ガス中ダ
イオキシン濃度を目標値(例えば、0.5 ng-TEQ/Nm3
以下)を満足し、しかも排出絶対量も少なくなる。ま
た、ダイオキシン含有粉塵の処理量も減る。更に、従来
の燃焼分解法のような二次燃焼設備が不要となり、また
そのランニングコストもかからない。このような効果を
発揮する製鋼用電気炉の排ガス処理方法及び装置を提供
することができ、工業上有用な効果がもたらされる。
As described above, according to the present invention,
In controlling the generation of dioxins contained in the gas generated from the electric furnace during the operation of the electric furnace for steelmaking, the cooling and dust collection system is not included when dioxin is contained in the exhaust gas (low-temperature exhaust gas) Since it is divided into cases (high-temperature exhaust gas), when the high-temperature exhaust gas is treated, dioxin does not come back from dust accumulated in a duct or the like due to the low-temperature exhaust gas treatment. Therefore, the concentration of dioxin in the exhaust gas emitted to the atmosphere is set to a target value (for example, 0.5 ng-TEQ / Nm 3
The following is satisfied, and the absolute emission is reduced. In addition, the processing amount of dioxin-containing dust is reduced. Further, secondary combustion equipment such as the conventional combustion decomposition method is not required, and the running cost is not required. An exhaust gas treatment method and apparatus for a steelmaking electric furnace exhibiting such effects can be provided, and industrially useful effects can be obtained.

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

【図1】この発明の電気炉の排ガス処理方法を実施する
ための排ガス処理装置例を示す概略フロー図である。
FIG. 1 is a schematic flow chart showing an example of an exhaust gas treatment apparatus for carrying out an electric furnace exhaust gas treatment method of the present invention.

【図2】この発明の電気炉の排ガス処理方法を実施する
ための排ガス処理装置の他の例を示す概略フロー図であ
る。
FIG. 2 is a schematic flow chart showing another example of an exhaust gas treatment apparatus for carrying out the electric furnace exhaust gas treatment method of the present invention.

【図3】従来の製鋼用電気炉の排ガス処理装置例の概略
フロー図である。
FIG. 3 is a schematic flowchart of an example of a conventional exhaust gas treatment apparatus for an electric furnace for steelmaking.

【符号の説明】[Explanation of symbols]

1 製鋼用電気炉 1a 排ガス 1b エルボ部 1c 摺動管 1d 集煙管 1e 排ガス 2 燃焼室 2’ 二次燃焼設備 3 水冷ダクト 4 排ガス温度指示制御装置 4a 排ガス 5 排ガス流路切替え装置 5a、5b 流量調節器 7 送風機 8 ガスホルダー 8a 排ガス 8b 排ガス温度指示計 9 水スプレー冷却塔 9a 排ガス 10、10’ 冷却装置 11 建屋集塵フード 11a 建屋集塵ガス 12、12’ 集塵装置 12a 排ガス 13 排風機 14 煙突 14a 排ガス 16、16’ 吸着剤吹込み装置 A、B 流路 DESCRIPTION OF SYMBOLS 1 Electric furnace for steel making 1a Exhaust gas 1b Elbow part 1c Sliding tube 1d Smoke collecting tube 1e Exhaust gas 2 Combustion chamber 2 'Secondary combustion facility 3 Water cooling duct 4 Exhaust gas temperature indication control device 4a Exhaust gas 5 Exhaust gas flow switching device 5a, 5b Flow rate control Device 7 Blower 8 Gas holder 8a Exhaust gas 8b Exhaust gas temperature indicator 9 Water spray cooling tower 9a Exhaust gas 10, 10 'Cooling device 11 Building dust collecting hood 11a Building dust collecting gas 12, 12' Dust collecting device 12a Exhaust gas 13 Exhaust gas 14 Chimney 14a Exhaust gas 16, 16 'Adsorbent injection device A, B Channel

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 製鋼用電気炉の操業過程で前記電気炉か
ら発生する高温の排ガスを燃焼室及び/又はダクトに導
き、前記排ガス中の未燃ガス成分を前記燃焼室及び/又
はダクトで燃焼させ、前記燃焼室及び/又はダクトから
排出された高温の排ガスを、冷却装置で冷却し、次いで
集塵装置に導き、前記排ガスを前記集塵装置で浄化処理
する製鋼用電気炉の排ガス処理方法において、 前記燃焼室及び/又はダクトから排出される前記排ガス
の温度がダイオキシンの燃焼分解温度に基づき予め定め
た一定値以上のときには、前記燃焼室及び/又はダクト
から排出された前記排ガスを、冷却装置に導きこの冷却
装置で冷却し、次いで前記冷却装置の下流に配設された
集塵装置にこの排ガスを導き、この集塵装置で浄化処理
し、そして、 前記燃焼室及び/又はダクトから排出される前記排ガス
の温度が、前記一定値未満のときには、前記燃焼室及び
/又はダクトから排出された前記排ガスを、前記冷却装
置を除く他の冷却装置に導きこの冷却装置で冷却し、次
いでこの冷却装置の下流に配設された集塵装置にこの排
ガスを導き、この集塵装置で浄化処理することを特徴と
する製鋼用電気炉の排ガス処理方法。
1. A high-temperature exhaust gas generated from an electric furnace during operation of an electric furnace for steelmaking is guided to a combustion chamber and / or a duct, and an unburned gas component in the exhaust gas is burned in the combustion chamber and / or a duct. And a high-temperature exhaust gas discharged from the combustion chamber and / or the duct is cooled by a cooling device, then guided to a dust collector, and the exhaust gas is purified by the dust collector. In the above, when the temperature of the exhaust gas discharged from the combustion chamber and / or the duct is equal to or higher than a predetermined value based on the combustion decomposition temperature of dioxin, the exhaust gas discharged from the combustion chamber and / or the duct is cooled. The exhaust gas is guided to a device, cooled by the cooling device, and then the exhaust gas is guided to a dust collecting device disposed downstream of the cooling device, purified by the dust collecting device, When the temperature of the exhaust gas discharged from the duct is less than the predetermined value, the exhaust gas discharged from the combustion chamber and / or the duct is guided to another cooling device except the cooling device, and the cooling device uses the exhaust gas. A method for treating an exhaust gas in an electric furnace for steelmaking, comprising cooling, then guiding the exhaust gas to a dust collector disposed downstream of the cooling device, and purifying the exhaust gas with the dust collector.
【請求項2】 製鋼用電気炉と、前記電気炉から発生す
る排ガス中の未燃ガス成分を燃焼させる燃焼室及び/又
はダクトと、前記燃焼室及び/又はダクトから排出され
る排ガス温度を測定し、この温度情報に基づき前記燃焼
室及び/又はダクトから排出された排ガスを次工程へ導
くべき排ガス流路を複数の排ガス流路の中から選定を
し、この選定結果に基づき前記排ガスを前記選定された
排ガス流路に導くための排ガス流路切替え機構と、前記
複数の排ガス流路の各々に通じて配設された前記排ガス
の冷却装置及びこの冷却装置の下流側に通じて配設され
た集塵装置からなる、複数の冷却・集塵装置系とを備え
たことを特徴とする、製鋼用電気炉の排ガス処理装置。
2. An electric furnace for steelmaking, a combustion chamber and / or duct for burning unburned gas components in exhaust gas generated from the electric furnace, and a temperature of exhaust gas discharged from the combustion chamber and / or duct. Then, based on this temperature information, an exhaust gas flow path from which the exhaust gas discharged from the combustion chamber and / or the duct is to be led to the next process is selected from among a plurality of exhaust gas flow paths. An exhaust gas passage switching mechanism for leading to a selected exhaust gas passage, a cooling device for the exhaust gas arranged to communicate with each of the plurality of exhaust gas passages, and a cooling device for the exhaust gas arranged downstream of the cooling device. An exhaust gas treating apparatus for an electric furnace for steelmaking, comprising a plurality of cooling / dust collecting systems each including a dust collecting device.
【請求項3】 請求項2記載の排ガス処理装置における
前記複数の排ガス流路と前記複数の冷却・集塵装置系と
の組合せからなる系の数は2である製鋼用電気炉の排ガ
ス処理装置を用い、請求項1記載の排ガス処理方法にお
けるダイオキシンの燃焼分解温度に基づき予め定めた前
記一定値は800℃であり、前記燃焼室及び/又はダク
トから排出される排ガス温度が800℃以上である場合
には常に一方の前記排ガス流路に導き、前記温度が80
0℃未満である場合には常に他方の前記排ガス流路に導
くことを特徴とする、請求項1記載の製鋼用電気炉の排
ガス処理方法。
3. The exhaust gas treatment apparatus for an electric furnace for steelmaking, wherein the number of systems comprising a combination of the plurality of exhaust gas passages and the plurality of cooling / dust collection systems in the exhaust gas treatment apparatus according to claim 2 is two. Wherein the predetermined value based on the combustion decomposition temperature of dioxin in the exhaust gas treatment method according to claim 1 is 800 ° C, and the temperature of the exhaust gas discharged from the combustion chamber and / or the duct is 800 ° C or higher. In such a case, the temperature is always led to one of the exhaust gas channels, and the temperature is set to 80.
2. The exhaust gas treatment method for an electric furnace for steelmaking according to claim 1, wherein when the temperature is lower than 0 [deg.] C., the exhaust gas is always led to the other exhaust gas channel.
JP9358452A 1997-12-25 1997-12-25 Method and device for treating exhaust gas of electric furnace for steel manufacture Pending JPH11190594A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9358452A JPH11190594A (en) 1997-12-25 1997-12-25 Method and device for treating exhaust gas of electric furnace for steel manufacture

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9358452A JPH11190594A (en) 1997-12-25 1997-12-25 Method and device for treating exhaust gas of electric furnace for steel manufacture

Publications (1)

Publication Number Publication Date
JPH11190594A true JPH11190594A (en) 1999-07-13

Family

ID=18459385

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9358452A Pending JPH11190594A (en) 1997-12-25 1997-12-25 Method and device for treating exhaust gas of electric furnace for steel manufacture

Country Status (1)

Country Link
JP (1) JPH11190594A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100418365B1 (en) * 2001-05-11 2004-02-11 주식회사 태양테크 Dual gas scrubber system
US7037356B2 (en) 2000-11-10 2006-05-02 Nippon Steel Corporation Method for operating rotary hearth type reducing furnace and rotary hearth type reducing furnace facilities
KR101159899B1 (en) * 2009-04-23 2012-06-26 현대제철 주식회사 System for processing of electric arc furnace combustion gas
EP3026126A4 (en) * 2013-07-24 2017-04-19 Nippon Steel & Sumitomo Metal Corporation Exhaust gas treatment method and exhaust gas treatment device
CN110801724A (en) * 2019-11-14 2020-02-18 西安交通大学 Flue gas pollutant desorption system with corrosion prevention and control function

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7037356B2 (en) 2000-11-10 2006-05-02 Nippon Steel Corporation Method for operating rotary hearth type reducing furnace and rotary hearth type reducing furnace facilities
KR100418365B1 (en) * 2001-05-11 2004-02-11 주식회사 태양테크 Dual gas scrubber system
KR101159899B1 (en) * 2009-04-23 2012-06-26 현대제철 주식회사 System for processing of electric arc furnace combustion gas
EP3026126A4 (en) * 2013-07-24 2017-04-19 Nippon Steel & Sumitomo Metal Corporation Exhaust gas treatment method and exhaust gas treatment device
US10612104B2 (en) 2013-07-24 2020-04-07 Nippon Steel Corporation Exhaust gas treatment method and exhaust gas treatment facility
CN110801724A (en) * 2019-11-14 2020-02-18 西安交通大学 Flue gas pollutant desorption system with corrosion prevention and control function
CN110801724B (en) * 2019-11-14 2023-12-19 西安交通大学 Flue gas pollutant removal system with corrosion prevention and control functions

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