JPH05222422A - Smelting reduction method for ore using coke packing layer type smelting reduction furnace - Google Patents
Smelting reduction method for ore using coke packing layer type smelting reduction furnaceInfo
- Publication number
- JPH05222422A JPH05222422A JP2124392A JP2124392A JPH05222422A JP H05222422 A JPH05222422 A JP H05222422A JP 2124392 A JP2124392 A JP 2124392A JP 2124392 A JP2124392 A JP 2124392A JP H05222422 A JPH05222422 A JP H05222422A
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- smelting reduction
- raw material
- material powder
- dust
- 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
Links
Landscapes
- Manufacture Of Iron (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、鉄鉱石等の有効金属の
酸化物を含む粉体を還元して、金属を製造するコークス
充填層型溶融還元炉を用いた鉱石の溶融還元方法に関す
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a smelting reduction method for ores using a coke packed bed type smelting reduction furnace for producing metal by reducing powder containing oxides of effective metals such as iron ore.
【0002】[0002]
【従来の技術】一般に、コークス充填層型溶融還元炉を
用いて金属を溶融還元する方法は図2に示すようなプロ
セスフローで行われる。他部門で発生したスラリー状の
原料粉はシツクナ23に供給され、底部に沈殿する。濃
縮したスラリー状の原料粉はポンプ(P)でデカンター
8に送られここで脱水され、更に濃縮された後スプレー
ドライヤ(乾燥機)10内に噴霧する。2. Description of the Related Art In general, a method for smelting and reducing a metal by using a coke packed bed type smelting reduction furnace is performed according to a process flow as shown in FIG. The slurry-like raw material powder generated in other departments is supplied to the honey 23 and settles at the bottom. The concentrated slurry-like raw material powder is sent to a decanter 8 by a pump (P), dehydrated there, further concentrated, and then sprayed into a spray dryer (dryer) 10.
【0003】一方、熱風発生装置11で生成した高温の
燃焼排ガスがスプレードライヤ10に吹込まれる。スプ
レードライヤ10内では、噴霧したスラリー状の原料粉
が吹込まれた高温の燃焼排ガスにより乾燥し、乾燥原料
粉となってスプレードライヤ10の底部に堆積する。ス
プレードライヤ10を通過した燃焼排ガスは次の集塵機
12で更に除塵され、煙突6から大気に放出される。On the other hand, high temperature combustion exhaust gas generated by the hot air generator 11 is blown into the spray dryer 10. In the spray dryer 10, the sprayed slurry-like raw material powder is dried by the high-temperature combustion exhaust gas blown therein, and becomes dry raw material powder and is deposited on the bottom of the spray dryer 10. The combustion exhaust gas that has passed through the spray dryer 10 is further dust-removed by the next dust collector 12, and is discharged from the chimney 6 to the atmosphere.
【0004】スプレードライヤ10及び集塵機12の底
部に堆積した乾燥した原料粉とダストは抜き取られ、貯
槽13に装入した後、均排圧ホッパ18とインジェクシ
ョンタンク25を通って、羽口15より竪型溶融還元炉
14に吹込まれる。吹込まれた原料粉は、溶融還元炉1
4内で還元され、溶融して金属21が製造される。この
溶融還元炉14はコークス16を充填した充填層型炉で
ある。The dry raw material powder and dust accumulated on the bottoms of the spray dryer 10 and the dust collector 12 are taken out, charged into the storage tank 13, and then passed through the uniform discharge pressure hopper 18 and the injection tank 25, and then vertically from the tuyere 15. It is blown into the mold smelting reduction furnace 14. The raw material powder blown into the smelting reduction furnace 1
It is reduced in 4 and melted to produce metal 21. This smelting reduction furnace 14 is a packed bed type furnace filled with coke 16.
【0005】竪型溶融還元炉14から排出する排ガスは
サイクロン17等の乾式除塵機により一次除塵されここ
で乾ダストを回収する。次に排ガスは二次除塵としてベ
ンチュリスクラバ22に送られ、散水し冷却する湿式除
塵が行われる。その後、シックナ5、及びデカンタ24
で処理され、湿ダストとして回収する。上記の乾ダスト
及び湿ダストは、現在焼結鉱用の原料として使用してい
る。Exhaust gas discharged from the vertical smelting reduction furnace 14 is subjected to primary dust removal by a dry dust remover such as a cyclone 17, and the dry dust is collected there. Next, the exhaust gas is sent to the venturi scrubber 22 as secondary dust removal, and wet dust removal is performed in which water is sprayed and cooled. Then Thickener 5 and Decanter 24
And is collected as wet dust. The above-mentioned dry dust and wet dust are currently used as raw materials for sinter.
【0006】除塵された清浄ガスはガス本管7でガスホ
ルダに送られCO含有ガスとして使用される。その一部
は熱風発生装置11に利用される。The decontaminated clean gas is sent to the gas holder in the gas main pipe 7 and used as a CO-containing gas. Part of it is used for the hot air generator 11.
【0007】[0007]
【発明が解決しようとする課題】前記の従来プロセスで
は次の問題があった。 (a)竪型溶融還元炉の排ガスを処理する除塵設備の建
設費が膨大である。 (b)またその設備の運転費及びメンテナンス費がかか
る。 (c)回収したダストの搬送費がかかる。 (d)高温の排ガス顕熱を回収することができず、エネ
ルギー損失が大きい。The above conventional process has the following problems. (A) The construction cost of the dust removing equipment for processing the exhaust gas of the vertical smelting reduction furnace is enormous. (B) In addition, operating costs and maintenance costs for the equipment are required. (C) The transportation cost of the collected dust is high. (D) High temperature exhaust gas sensible heat cannot be recovered, resulting in large energy loss.
【0008】本発明は以上の問題点を解決した排ガス顕
熱の有効利用(回収)と排ガス中のダストの捕集(回
収)を同時に行う技術を提供することを目的とする。It is an object of the present invention to provide a technique for solving the above problems and effectively utilizing (recovering) exhaust gas sensible heat and collecting (recovering) dust in exhaust gas at the same time.
【0009】[0009]
【課題を解決するための手段】本発明は、前記の問題点
を解決するためになされたもので、竪型溶融還元炉から
排出した排ガスを原料粉乾燥機(スプレードライヤ)に
直接供給し、排ガス顕熱を利用してスラリー状の原料粉
を乾燥させると共に、排ガス中のダストを原料粉に吸着
させて回収し、回収した排ガス中のダストを原料粉と共
に溶融還元炉に戻すようにしたものである。The present invention has been made to solve the above-mentioned problems, in which exhaust gas discharged from a vertical smelting reduction furnace is directly supplied to a raw material powder dryer (spray dryer), Slurry raw material powder is dried by utilizing sensible heat of exhaust gas, and dust in exhaust gas is adsorbed to the raw material powder and collected, and the collected dust in exhaust gas is returned to the melting reduction furnace together with the raw material powder. Is.
【0010】[0010]
【作用】本発明では、竪型溶融還元炉の排ガスを湿式除
塵機等を通過させることなく、原料粉乾燥機に導き、そ
の保有熱によって原料を乾燥し、一方原料粉によってガ
ス中のダストを集塵し回収する。このため、溶融還元炉
の排ガスの湿式除塵装置が不要となり、原料粉を乾燥す
るための別途の熱源も不要となる。また、排ガス中のダ
ストは原料粉に吸着され、これと共に排出されるので粉
塵処理のためのシステムが不要となる。In the present invention, the exhaust gas of the vertical smelting reduction furnace is introduced into the raw material powder dryer without passing through the wet dust remover and the raw material is dried by the heat retained therein, while the dust in the gas is removed by the raw material powder. Collect and collect dust. Therefore, a wet dust remover for exhaust gas of the smelting reduction furnace is not required, and a separate heat source for drying the raw material powder is also unnecessary. Further, since the dust in the exhaust gas is adsorbed by the raw material powder and discharged together with it, a system for dust treatment is not required.
【0011】[0011]
【実施例】本発明の実施例を図1のプロセスフロー図に
よって以下に説明する。他部門で発生したスラリー状の
原料粉がシツクナ23に供給され、デカンタ8に送ら
れ、脱水、濃縮された後、スプレードライヤ10内に噴
霧することは図2と同様である。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT An embodiment of the present invention will be described below with reference to the process flow diagram of FIG. It is the same as in FIG. 2 that the slurry-like raw material powder generated in another department is supplied to the shucker 23, sent to the decanter 8, dehydrated and concentrated, and then sprayed in the spray dryer 10.
【0012】実施例では、竪型溶融還元炉14により排
出した排ガスをスプレードライヤ10に直接供給すると
ころが図2と異なっている。スプレードライヤ10内で
は噴霧されスラリー状の原料粉が高温の排ガスにより乾
燥され、乾燥原料粉となり排ガス中のダストを吸着、捕
集し、スプレードライヤ10の底部に堆積する。The embodiment differs from FIG. 2 in that the exhaust gas discharged from the vertical smelting reduction furnace 14 is directly supplied to the spray dryer 10. In the spray dryer 10, the slurry-like raw material powder is dried by the high-temperature exhaust gas, becomes dry raw material powder, adsorbs and collects the dust in the exhaust gas, and deposits on the bottom of the spray dryer 10.
【0013】スプレードライヤ10を通過した排ガスは
次の集塵機12で更に除塵された後、ガス本管7により
ガスホルダに送られ使用される。その一部は熱風発生装
置11で利用される。スプレードライヤ10と集塵機1
2の底部に堆積した乾燥した原料粉とダストは下部より
抜き取り、貯槽13に装入した後、均排圧ホッパ18と
インジェクションタンク25を通り、羽口15より竪型
溶融還元炉14内に吹込まれる。The exhaust gas that has passed through the spray dryer 10 is further dust-removed by the next dust collector 12, and then sent to the gas holder by the gas main pipe 7 for use. A part of it is used in the hot air generator 11. Spray dryer 10 and dust collector 1
The dry raw material powder and dust accumulated on the bottom of No. 2 are extracted from the lower part, charged into the storage tank 13, and then passed through the pressure equalizing hopper 18 and the injection tank 25 and blown from the tuyere 15 into the vertical melting and reduction furnace 14. Get caught.
【0014】本発明は、上記のようなプロセスにしたこ
とにより、スプレードライヤ10で溶融還元炉の高温の
排ガス顕熱を有効利用してスラリー状の原料粉を乾燥
し、同時に排ガス中のダストを吸着・捕集(回収)する
ことができる。竪型溶融還元炉14から排出した排ガス
の温度は炉頂部で約750℃(max約900℃)で、
排ガス量は約26000Nm3 /Hを示し、含塵濃度は
約30〜50g/Nm3 の範囲にあった。この排ガス
は、スプレードライヤ10に送られ、スプレードライヤ
10内に噴霧した約2100kg/H(含水率約50
%)のスラリー状の原料粉を乾燥し、温度が約180℃
以下に低下した。また、排ガスは次の集塵機12で約
0.5mg/Nm3 まで良好に除塵された。According to the present invention, by adopting the above-described process, the slurry dryer raw material powder is dried by the spray dryer 10 by effectively utilizing the high temperature exhaust gas sensible heat of the smelting reduction furnace, and at the same time, the dust in the exhaust gas is removed. Can be adsorbed and collected (collected). The temperature of the exhaust gas discharged from the vertical smelting reduction furnace 14 is about 750 ° C. (max about 900 ° C.) at the furnace top,
The amount of exhaust gas was about 26000 Nm 3 / H, and the dust concentration was in the range of about 30 to 50 g / Nm 3 . This exhaust gas is sent to the spray dryer 10 and sprayed into the spray dryer 10 at about 2100 kg / H (water content of about 50
%) Slurry raw material powder is dried and the temperature is about 180 ° C.
Fell below. The exhaust gas was satisfactorily removed by the next dust collector 12 to about 0.5 mg / Nm 3 .
【0015】一方、スプレードライヤ10及び集塵機1
2で捕集(回収)した乾燥した原料粉とダストは下部よ
り抜き取り貯槽13に装入した後均排圧ホッパ18とイ
ンジェクションタンク25を通し、羽口15より竪型溶
融還元炉14に吹込み、問題なく操業を行った。On the other hand, the spray dryer 10 and the dust collector 1
The dried raw material powder and dust collected (recovered) in 2 are withdrawn from the lower portion, charged into the storage tank 13, and then passed through the pressure equalizing hopper 18 and the injection tank 25 and blown into the vertical melting and reducing furnace 14 from the tuyere 15. , Operated without problems.
【0016】[0016]
【発明の効果】本発明はコークス充填層型溶融還元炉か
ら排出する高温の排ガスを乾燥機に直接供給し、排ガス
の顕熱をスラリー状の原料粉の乾燥用熱源として利用し
たことにより原料粉の乾燥と排熱回収が良好に行われ
た。また、排ガス中のダストを良好に捕集(回収)する
ことができた。INDUSTRIAL APPLICABILITY According to the present invention, the high temperature exhaust gas discharged from the coke packed bed type smelting reduction furnace is directly supplied to the dryer, and the sensible heat of the exhaust gas is used as a heat source for drying the slurry raw material powder. The drying and recovery of waste heat were performed well. Further, the dust in the exhaust gas could be collected (recovered) well.
【0017】上記の結果、本発明の実施により、従来の
プロセスでは必要であった、サイクロン(又は除塵
器)、ベンチュリスクラバ、シツクナ等の排ガス処理設
備が不要になった。また、それらの設備の運転費とメン
テナンス費、回収したダストの輸送費等が不要となっ
た。更に、竪型溶融還元炉で使用するコークスの使用量
が低減した等の効果を得た。As a result of the above, by implementing the present invention, exhaust gas treatment equipment such as a cyclone (or dust remover), a venturi scrubber, and a sychna, which is required in the conventional process, is no longer required. In addition, operating costs and maintenance costs for these facilities, transportation costs for collected dust, etc. have become unnecessary. Furthermore, effects such as a reduction in the amount of coke used in the vertical smelting reduction furnace were obtained.
【0018】本発明の応用としてサイクロン(または除
塵器)は従来のプロセスと同様に配置し、ベンチュリス
クラバ、シツクナ等の湿式集塵機のみを不要にすること
によっても相当量の効果がある。As an application of the present invention, the cyclone (or dust remover) is arranged in the same manner as in the conventional process, and the wet dust collector such as the venturi scrubber and the shredder is not required, and the effect is considerable.
【図1】本発明の実施例のプロセスを示すフロー図であ
る。FIG. 1 is a flow diagram illustrating a process of an embodiment of the present invention.
【図2】従来のプロセスを示すフロー図である。FIG. 2 is a flow chart showing a conventional process.
5 シックナ 6 煙突 7 ガス本管 8 デカ
ンタ 10 スプレードライヤ(乾燥機) 11 熱風
発生装置 12 集塵機 13 貯槽 14 竪型溶融還元炉 15 羽口 16 充填層 17 サイ
クロン又は除塵器 18 均排圧ホッパ 20 送風
機 21 金属 22 ベン
チュリスクラバ 23 シックナ 24 デカ
ンタ 25 インジェクションタンク 26 環水
冷却・循環設備 27 熱交換器 28 送風
機5 Thickener 6 Chimney 7 Gas main 8 Decanter 10 Spray dryer (dryer) 11 Hot air generator 12 Dust collector 13 Storage tank 14 Vertical smelting reduction furnace 15 Tuyere 16 Packed layer 17 Cyclone or dust remover 18 Uniform discharge hopper 20 Blower 21 Metal 22 Venturi scrubber 23 Thickener 24 Decanter 25 Injection tank 26 Ring water cooling / circulation equipment 27 Heat exchanger 28 Blower
───────────────────────────────────────────────────── フロントページの続き (72)発明者 相原 恒雄 千葉市川崎町1番地 川崎製鉄株式会社千 葉製鉄所内 (72)発明者 長谷川 恒也 千葉市川崎町1番地 川崎製鉄株式会社千 葉製鉄所内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Tsuneo Aihara 1 Kawasaki-cho, Chiba City Inside the Chiba Steel Works, Kawasaki Steel Co., Ltd. (72) Tsuneya Hasegawa 1 Kawasaki-cho, Chiba City Inside the Chiba Steel Works, Kawasaki Steel Co., Ltd.
Claims (1)
を還元し金属を製造するコークス充填層型溶融還元炉の
還元方法において、竪型溶融還元炉から排出する高温排
ガスを原料粉乾燥機に直接供給し、排ガスの顕熱を利用
してスラリー状の原料粉を乾燥すると共に、排ガス中の
ダストを原料粉に吸着させて回収し、排ガス中のダスト
を原料粉と共に、溶融還元炉に戻すことを特徴とするコ
ークス充填層型溶融還元炉を用いた鉱石の溶融還元方
法。1. In a reduction method of a coke packed bed type smelting reduction furnace for producing a metal by reducing a powder containing oxides of an effective metal such as iron ore, high temperature exhaust gas discharged from a vertical smelting reduction furnace is used as a raw material powder. Directly supply to the dryer, dry the slurry-like raw material powder by utilizing the sensible heat of the exhaust gas, adsorb the dust in the exhaust gas to the raw material powder and collect it, and melt and reduce the dust in the exhaust gas together with the raw material powder. A method for smelting reduction of ore using a coke packed bed type smelting reduction furnace characterized by returning to the furnace.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2124392A JPH05222422A (en) | 1992-02-06 | 1992-02-06 | Smelting reduction method for ore using coke packing layer type smelting reduction furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2124392A JPH05222422A (en) | 1992-02-06 | 1992-02-06 | Smelting reduction method for ore using coke packing layer type smelting reduction furnace |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH05222422A true JPH05222422A (en) | 1993-08-31 |
Family
ID=12049617
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2124392A Pending JPH05222422A (en) | 1992-02-06 | 1992-02-06 | Smelting reduction method for ore using coke packing layer type smelting reduction furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH05222422A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1997036012A1 (en) * | 1996-03-27 | 1997-10-02 | Georg Fischer Disa Engineering Ag | Process for recovering and disposing of residues produced in cupola furnaces |
KR20200056718A (en) * | 2018-11-15 | 2020-05-25 | 황연수 | Apparatus for processing dust using spary dryer |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01129917A (en) * | 1987-11-13 | 1989-05-23 | Kawasaki Heavy Ind Ltd | Device for preheating and charging material in reduction furnace |
JPH04110408A (en) * | 1990-08-31 | 1992-04-10 | Nkk Corp | Smelting-reduction method and equipment for iron ore |
JPH04110409A (en) * | 1990-08-31 | 1992-04-10 | Nkk Corp | Smelting-reduction method and equipment for iron ore |
-
1992
- 1992-02-06 JP JP2124392A patent/JPH05222422A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01129917A (en) * | 1987-11-13 | 1989-05-23 | Kawasaki Heavy Ind Ltd | Device for preheating and charging material in reduction furnace |
JPH04110408A (en) * | 1990-08-31 | 1992-04-10 | Nkk Corp | Smelting-reduction method and equipment for iron ore |
JPH04110409A (en) * | 1990-08-31 | 1992-04-10 | Nkk Corp | Smelting-reduction method and equipment for iron ore |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1997036012A1 (en) * | 1996-03-27 | 1997-10-02 | Georg Fischer Disa Engineering Ag | Process for recovering and disposing of residues produced in cupola furnaces |
KR20200056718A (en) * | 2018-11-15 | 2020-05-25 | 황연수 | Apparatus for processing dust using spary dryer |
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A02 | Decision of refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A02 Effective date: 19970204 |