JPH11342314A - Treatment of chloride dust containing-exhaust gas and treating device therefor - Google Patents
Treatment of chloride dust containing-exhaust gas and treating device thereforInfo
- Publication number
- JPH11342314A JPH11342314A JP10169209A JP16920998A JPH11342314A JP H11342314 A JPH11342314 A JP H11342314A JP 10169209 A JP10169209 A JP 10169209A JP 16920998 A JP16920998 A JP 16920998A JP H11342314 A JPH11342314 A JP H11342314A
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- duct
- dust
- chloride dust
- chloride
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
Landscapes
- Treating Waste Gases (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は塩化物ダスト含有排
ガスの処理方法および処理装置に関し、特に、ダクトや
バグフィルタの目詰まりを効果的に防止できる塩化物ダ
スト含有排ガスの処理方法および処理装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for treating exhaust gas containing chloride dust, and more particularly to a method and an apparatus for treating exhaust gas containing chloride dust which can effectively prevent clogging of ducts and bag filters. .
【0002】[0002]
【従来の技術】製鉄ダストを還元して再利用を図る還元
用回転炉床炉の排ガス中には、装入材料に起因するZn
のヒュームが多く含まれ、このZnは通常ZnOとなっ
て排ガス中にダストとして存在する。また、ダスト中に
は塩素(Cl)が含まれているためZnC12 が生成さ
れる。ZnCl2 は融点が400℃程度、沸点が700
℃程度であって、この温度範囲では液相を呈し、排気ダ
クトやバグフィルタに付着して目詰まりを生じさせる原
因となる。2. Description of the Related Art The exhaust gas from a rotary hearth furnace for reduction, which aims to reuse iron dust by reducing it, contains Zn originating from charged materials.
This Zn is usually contained in the exhaust gas as dust and becomes ZnO. Further, since chlorine (Cl) is contained in the dust, ZnC12 is generated. ZnCl 2 has a melting point of about 400 ° C. and a boiling point of 700
It is about ° C., and in this temperature range, it exhibits a liquid phase and adheres to the exhaust duct and the bag filter to cause clogging.
【0003】そこで、従来、炉から排出された1200
℃程度の排ガスを、耐火物を内張りしたダクトにより冷
却塔へ導き、ここで冷風と混合して気相の排ガスをダス
ト(ZnC12 )の融点以下へ急速冷却して固相にする
ことが行われている。しかし、この方法では、高温の排
ガスを急速に冷却するために大量の冷風を吹き込む必要
があり、排ガスの全量が増大して、後段に設けられる集
塵機や排風機の容量が過大なものになるという問題があ
る。また、高温の排ガスが流通するダクトの内面に、焼
き付きによってダストが強固に付着してしまうという問
題もある。[0003] Therefore, conventionally, the 1200
The exhaust gas of about ℃ is led to a cooling tower through a duct lined with refractory material, where it is mixed with cold air to rapidly cool the gaseous exhaust gas to the melting point of dust (ZnC12) or less to form a solid phase. ing. However, in this method, it is necessary to blow a large amount of cold air in order to rapidly cool the high-temperature exhaust gas, and the total amount of the exhaust gas increases, and the capacity of the dust collector and the exhaust fan provided at the subsequent stage becomes excessive. There's a problem. Further, there is also a problem that dust adheres firmly to the inner surface of the duct through which high-temperature exhaust gas flows due to seizure.
【0004】排ガス全量の増大を抑えるために、冷却塔
内で排ガスに水や水蒸気を直接吹き掛けてその気化潜熱
によって排ガスを急冷する方法も試みられているが、固
相になったZnC12 を多く含むダストは潮解性を有す
るため水分を吸収して流動化し、ダクトやバグフィルタ
の目詰まりを生じさせ易いとともに、排ガスの露点が高
くなるため集塵機およびこれに至るダクトを保温しない
と結露を生じるという問題がある。In order to suppress an increase in the total amount of exhaust gas, a method of directly spraying water or steam on the exhaust gas in a cooling tower to quench the exhaust gas by the latent heat of vaporization thereof has been attempted. However, ZnC12 in a solid phase is often used. The dust contains deliquescent so that it absorbs and fluidizes water, making it easy to clog ducts and bag filters.In addition, the dew point of exhaust gas is high, so dew forms unless the dust collector and the duct leading to it are kept warm. There's a problem.
【0005】[0005]
【発明が解決しようとする課題】そこで本発明は上記従
来技術の課題を解決するもので、集塵機や排風機の容量
増大や結露防止のためのダクトの保温施工を行うことな
く、排気ダクトやバグフィルタの目詰まりを完全に防止
することができる塩化物ダスト含有排ガスの処理方法お
よび処理装置を提供することを目的とする。SUMMARY OF THE INVENTION The present invention solves the above-mentioned problems of the prior art. In order to increase the capacity of a dust collector or an exhaust fan or to perform heat insulation of a duct for preventing dew condensation, an exhaust duct or a bug is prevented. An object of the present invention is to provide a method and an apparatus for treating exhaust gas containing chloride dust, which can completely prevent clogging of a filter.
【0006】[0006]
【課題を解決するための手段】上記目的を達成するた
め、本発明の塩化物ダスト含有排ガスの処理方法では、
塩化物ダストを含む排ガスを、隔壁を介した熱交換によ
り上記塩化物ダストの沸点に近くかつ当該沸点よりも高
い温度まで予備冷却し、その後、上記排ガスに冷風を混
入して当該排ガスを上記塩化物ダストの融点よりも低い
温度へ急速冷却することを特徴としている。In order to achieve the above object, the method for treating exhaust gas containing chloride dust according to the present invention comprises:
The exhaust gas containing chloride dust is pre-cooled to a temperature close to the boiling point of the chloride dust and higher than the boiling point by heat exchange through a partition wall. It is characterized by rapid cooling to a temperature lower than the melting point of material dust.
【0007】本発明の方法においては、冷風を混入する
までに、隔壁を介した熱交換により排ガスの温度は塩化
物ダストの沸点近くまで予め低下させられている。した
がって、従来のような大量の冷風を供給しなくても、排
ガス温度は速やかに塩化物ダストの融点よりも低い温度
へ低下する。この結果、塩化物ダストは液相を速やかに
通過して固相になり、ダクト等の目詰まりが回避され
る。この場合、上述のように冷風の供給量を少なくでき
るから、集塵機や排風機の容量が必要以上に大きくなる
ことはない。さらに、従来のように、急速冷却のために
水や水蒸気を直接排ガスに混入させることもないから、
塩化物ダストの流動化が阻止され、これによってもダク
ト等の目詰まりが防止されるとともに、排ガスの露点が
上昇しないから集塵機およびこれに至るダクトの保温施
工も不要となる。[0007] In the method of the present invention, the temperature of the exhaust gas is previously reduced to near the boiling point of chloride dust by heat exchange through the partition before the cold air is mixed. Therefore, even if a large amount of cold air is not supplied as in the related art, the temperature of the exhaust gas quickly drops to a temperature lower than the melting point of chloride dust. As a result, the chloride dust quickly passes through the liquid phase to become a solid phase, thereby preventing clogging of the duct and the like. In this case, since the supply amount of the cool air can be reduced as described above, the capacity of the dust collector and the exhaust fan does not increase more than necessary. Furthermore, unlike the conventional case, water and steam are not directly mixed into the exhaust gas for rapid cooling.
Fluidization of chloride dust is prevented, which also prevents clogging of the duct and the like, and the dew point of the exhaust gas does not rise, so that it is not necessary to heat-protect the dust collector and the duct leading to the dust collector.
【0008】また、上記処理方法は、以下の処理装置に
よって実現することができる。すなわち、塩化物ダスト
含有排ガスの処理装置は、工業炉(1)から排出される
塩化物ダストを含む排ガスを流通させて、上記塩化物ダ
ストの沸点に近くかつ当該沸点よりも高い温度まで排ガ
スを予備冷却する冷却ダクト(2)と、当該冷却ダクト
(2)を通過した上記排ガスに冷風を供給して排ガスを
上記塩化物ダストの融点よりも低い温度へ急速冷却する
冷却塔(3)とを具備している。[0008] The above processing method can be realized by the following processing apparatus. That is, the apparatus for treating exhaust gas containing chloride dust circulates the exhaust gas containing chloride dust discharged from the industrial furnace (1), and exhausts the exhaust gas to a temperature close to and higher than the boiling point of the chloride dust. A cooling duct (2) for pre-cooling, and a cooling tower (3) for supplying cool air to the exhaust gas passing through the cooling duct (2) and rapidly cooling the exhaust gas to a temperature lower than the melting point of the chloride dust. I have it.
【0009】上記工業炉(1)と冷却ダクト(2)との
間に排ガスの顕熱を利用する熱交換器(10)を設ける
ことができる。これによれば、排ガスの冷却と同時に排
熱の有効利用を図ることができる。[0009] A heat exchanger (10) utilizing sensible heat of exhaust gas can be provided between the industrial furnace (1) and the cooling duct (2). According to this, the exhaust heat can be effectively used simultaneously with the cooling of the exhaust gas.
【0010】なお、上記カッコ内の符号は、後述する実
施形態に記載の具体的手段との対応関係を示すものであ
る。[0010] The reference numerals in parentheses indicate the correspondence with specific means described in the embodiment described later.
【0011】[0011]
【発明の実施の形態】(第1実施形態)図1には本発明
の処理方法を実施する処理装置の一例を示す。製鉄ダス
ト還元用の回転炉床炉1からは水冷ダクト2が冷却塔3
まで延び、この水冷ダクト2内を、ZnO及びZnCl
2 をダストとして含む排ガスが流通させられる。水冷ダ
クト2の内周面温度は100〜150℃程度であり、1
200℃程度の高温で回転炉床炉1から流出した排ガス
は水冷ダクト2を流通する間に放熱して予備冷却され、
冷却塔3に至る時にはZnCl2 の沸点(約700℃)
に近くかつこれよりもやや高い750℃程度までその温
度が低下する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS (First Embodiment) FIG. 1 shows an example of a processing apparatus for performing a processing method of the present invention. From the rotary hearth furnace 1 for reducing ironmaking dust, a water-cooled duct 2 is
And extends through the water-cooled duct 2 with ZnO and ZnCl
Exhaust gas containing 2 as dust is distributed. The inner peripheral surface temperature of the water cooling duct 2 is about 100 to 150 ° C.
Exhaust gas flowing out of the rotary hearth furnace 1 at a high temperature of about 200 ° C. radiates heat while flowing through the water cooling duct 2 and is pre-cooled,
When reaching the cooling tower 3, the boiling point of ZnCl2 (about 700 ° C)
The temperature drops to about 750 ° C., which is close to and slightly higher than this.
【0012】冷却塔3にはエアダンパ71を介設したエ
アダクト7によって30℃程度の冷風が供給されてお
り、この冷風の混入によって排ガスはZnCl2 の融点
(約400℃)よりも低い250℃以下へ急速に冷却さ
れる。この結果、排ガス中のZnCl2 は気相から液相
を速やかに通過して固相になる。また、この温度域では
ZnOも固相となる。Cooling air of about 30 ° C. is supplied to the cooling tower 3 by an air duct 7 having an air damper 71 interposed therebetween. Cools rapidly. As a result, ZnCl2 in the exhaust gas quickly passes from the gas phase to the liquid phase to become a solid phase. In this temperature range, ZnO also becomes a solid phase.
【0013】固相となったZnOおよびZnCl2 を含
む排ガスは排気ダクト8を経て集塵機4に至り、内蔵さ
れたバグフィルタで捕集されて浄化された後、排風機5
を経て煙突6から排出される。この間、ZnO及びZn
Cl2 は乾燥した固体となっているから、排気ダクト8
や集塵機4内のバグフィルタに付着しても目詰まり等の
原因になることはない。The exhaust gas containing the solid phase of ZnO and ZnCl 2 reaches the dust collector 4 via the exhaust duct 8 and is collected and purified by the built-in bag filter.
Through the chimney 6. During this time, ZnO and Zn
Since Cl2 is a dry solid, the exhaust duct 8
Even if it adheres to the bag filter in the dust collector 4, it does not cause clogging or the like.
【0014】(第2実施形態)図2に示すように、回転
炉床炉1から出た直後のダクト9中に流通抵抗の小さい
輻射型の熱交換器10を設けて、空気との間で熱交換さ
せるようにしても良い。すなわち、回転炉床炉1から排
出された排ガスの熱で熱交換器10に供給される空気を
加熱して回転炉床炉1で使用される予熱空気にする。そ
して、この間に排ガスの熱を奪ってその温度を回転炉床
炉1から流出する際の1200℃程度から1000℃程
度まで低下させ、温度低下した排ガスを冷却塔3に至る
水冷ダクト2に導入する。これによれば、水冷ダクトを
短くできるとともに、排熱の有効利用を図ることができ
る。(Second Embodiment) As shown in FIG. 2, a radiant heat exchanger 10 having a small flow resistance is provided in a duct 9 immediately after exiting from a rotary hearth furnace 1, so that it can be connected to air. Heat exchange may be performed. That is, the air supplied to the heat exchanger 10 is heated by the heat of the exhaust gas discharged from the rotary hearth furnace 1 to be preheated air used in the rotary hearth furnace 1. During this time, the exhaust gas is deprived of heat and its temperature is lowered from about 1200 ° C. when flowing out of the rotary hearth furnace 1 to about 1000 ° C., and the exhaust gas whose temperature has dropped is introduced into the water cooling duct 2 leading to the cooling tower 3. . According to this, the water cooling duct can be shortened, and effective use of exhaust heat can be achieved.
【0015】なお、本発明の対象となる塩化物ダストは
Znを含むダストに限られず例えばPbを含むようなダ
ストにも適用できる。また、排ガス温度を沸点近くまで
低下させるのに上記各実施形態では水冷ダクトを使用し
たが、冷媒が排ガスに直接混入せず隔壁を介して熱交換
するものであれば、水冷ダクトには限られない。It should be noted that the chloride dust to which the present invention is applied is not limited to dust containing Zn but can be applied to dust containing Pb, for example. Further, in each of the above embodiments, a water-cooled duct was used to lower the exhaust gas temperature to near the boiling point.However, as long as the refrigerant does not directly mix with the exhaust gas and exchanges heat through the partition, the water-cooled duct is limited. Absent.
【0016】[0016]
【発明の効果】以上のように、本発明によれば、排ガス
中のダストによるダクトやバグフィルタの目詰まりを完
全に防止することができるとともに、集塵機や排風機の
容量増大や結露防止のためのダクトの保温施工等が不要
となり、大幅なコスト低減を実現することができる。As described above, according to the present invention, it is possible to completely prevent the clogging of the duct and the bag filter due to the dust in the exhaust gas, and to increase the capacity of the dust collector and the exhaust fan and to prevent dew condensation. This eliminates the need for heat-retaining work for the duct, and can realize a significant cost reduction.
【図1】本発明の第1実施形態における、処理装置の系
統図である。FIG. 1 is a system diagram of a processing apparatus according to a first embodiment of the present invention.
【図2】本発明の第2実施形態における、処理装置の系
統図である。FIG. 2 is a system diagram of a processing device according to a second embodiment of the present invention.
1…回転炉床炉、2…水冷ダクト、3…冷却塔、4…集
塵機、7…エアダクト、8…排気ダクト、10…熱交換
器。DESCRIPTION OF SYMBOLS 1 ... Rotary hearth furnace, 2 ... Water cooling duct, 3 ... Cooling tower, 4 ... Dust collector, 7 ... Air duct, 8 ... Exhaust duct, 10 ... Heat exchanger.
Claims (3)
した熱交換により前記塩化物ダストの沸点に近くかつ当
該沸点よりも高い温度まで予備冷却し、その後、前記排
ガスに冷風を混入して当該排ガスを前記塩化物ダストの
融点よりも低い温度へ急速冷却することを特徴とする塩
化物ダスト含有排ガスの処理方法。1. Exhaust gas containing chloride dust is pre-cooled to a temperature close to and higher than the boiling point of the chloride dust by heat exchange through a partition, and thereafter, cool air is mixed into the exhaust gas. A method for treating an exhaust gas containing chloride dust, wherein the exhaust gas is rapidly cooled to a temperature lower than the melting point of the chloride dust.
む排ガスを流通させて、前記塩化物ダストの沸点に近く
かつ沸点よりも高い温度まで排ガスを予備冷却する冷却
ダクトと、当該冷却ダクトを通過した前記排ガスに冷風
を供給して排ガスを前記塩化物ダストの融点よりも低い
温度へ急速冷却する冷却塔とを具備する塩化物ダスト含
有排ガスの処理装置。2. A cooling duct for pre-cooling exhaust gas containing chloride dust discharged from an industrial furnace to a temperature close to and higher than the boiling point of the chloride dust, and a cooling duct for cooling the exhaust gas. A cooling tower for supplying cool air to the passed exhaust gas to rapidly cool the exhaust gas to a temperature lower than the melting point of the chloride dust, and a cooling tower for treating the exhaust gas containing chloride dust.
記排ガスの顕熱を利用する熱交換器を設けた請求項2に
記載の塩化物ダスト含有排ガスの処理装置。3. An apparatus for treating exhaust gas containing chloride dust according to claim 2, wherein a heat exchanger utilizing sensible heat of said exhaust gas is provided between said industrial furnace and said cooling duct.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16920998A JP3864564B2 (en) | 1998-06-01 | 1998-06-01 | Method and apparatus for treating exhaust gas containing chloride dust |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16920998A JP3864564B2 (en) | 1998-06-01 | 1998-06-01 | Method and apparatus for treating exhaust gas containing chloride dust |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH11342314A true JPH11342314A (en) | 1999-12-14 |
JP3864564B2 JP3864564B2 (en) | 2007-01-10 |
Family
ID=15882234
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP16920998A Expired - Fee Related JP3864564B2 (en) | 1998-06-01 | 1998-06-01 | Method and apparatus for treating exhaust gas containing chloride dust |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3864564B2 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002038815A1 (en) * | 2000-11-10 | 2002-05-16 | Nippon Steel Corporation | Method for operating rotary hearth type reducing furnace and rotary hearth type reducing furnace facilities |
CN100355911C (en) * | 2000-11-10 | 2007-12-19 | 新日本制铁株式会社 | Method for operating rotary hearth type reducing furnace and rotary hearth type reducing furnace facilities |
WO2009008256A1 (en) | 2007-07-10 | 2009-01-15 | Kabushiki Kaisha Kobe Seiko Sho | Apparatus and method for treating waste gas for rotary hearth furnace-type reducing furnace |
JP2009281617A (en) * | 2008-05-20 | 2009-12-03 | Nippon Steel Engineering Co Ltd | Exhaust gas treatment method for rotary hearth furnace |
-
1998
- 1998-06-01 JP JP16920998A patent/JP3864564B2/en not_active Expired - Fee Related
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002038815A1 (en) * | 2000-11-10 | 2002-05-16 | Nippon Steel Corporation | Method for operating rotary hearth type reducing furnace and rotary hearth type reducing furnace facilities |
EP1340822A4 (en) * | 2000-11-10 | 2006-04-05 | Nippon Steel Corp | Method for operating rotary hearth type reducing furnace and rotary hearth type reducing furnace facilities |
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 |
CN100355911C (en) * | 2000-11-10 | 2007-12-19 | 新日本制铁株式会社 | Method for operating rotary hearth type reducing furnace and rotary hearth type reducing furnace facilities |
WO2009008256A1 (en) | 2007-07-10 | 2009-01-15 | Kabushiki Kaisha Kobe Seiko Sho | Apparatus and method for treating waste gas for rotary hearth furnace-type reducing furnace |
JP2009019786A (en) * | 2007-07-10 | 2009-01-29 | Kobe Steel Ltd | Device and method for exhaust gas treatment of rotary hearth-type reducing furnace |
JP2009281617A (en) * | 2008-05-20 | 2009-12-03 | Nippon Steel Engineering Co Ltd | Exhaust gas treatment method for rotary hearth furnace |
Also Published As
Publication number | Publication date |
---|---|
JP3864564B2 (en) | 2007-01-10 |
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