发明公开
- 专利标题: VERFAHREN ZUM HERSTELLEN VON FLÜSSIGEM ROHEISEN ODER FLÜSSIGEN STAHLVORPRODUKTEN
- 专利标题(英): Method of producing liquid pig iron or liquid steel precursors
- 专利标题(中): 法生产液态生铁或钢液前兆
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申请号: EP97928042.0申请日: 1997-06-26
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公开(公告)号: EP0914475A1公开(公告)日: 1999-05-12
- 发明人: KEPPLINGER, Leopold, Werner , WALLNER, Felix , SCHENK, Johannes , LEE, Il-Ock , KIM, Yong-Ha , PARK, Moon, Duk
- 申请人: VOEST-ALPINE INDUSTRIEANLAGENBAU GMBH , POHANG IRON & STEEL CO., LTD. , RESEARCH INSTITUTE OF INDUSTRIAL SCIENCE & TECHNOLOGY, INCORPORATED FOUNDATION
- 申请人地址: Turmstrasse 44 4020 Linz AT
- 专利权人: VOEST-ALPINE INDUSTRIEANLAGENBAU GMBH,POHANG IRON & STEEL CO., LTD.,RESEARCH INSTITUTE OF INDUSTRIAL SCIENCE & TECHNOLOGY, INCORPORATED FOUNDATION
- 当前专利权人: VOEST-ALPINE INDUSTRIEANLAGENBAU GMBH,POHANG IRON & STEEL CO., LTD.,RESEARCH INSTITUTE OF INDUSTRIAL SCIENCE & TECHNOLOGY, INCORPORATED FOUNDATION
- 当前专利权人地址: Turmstrasse 44 4020 Linz AT
- 代理机构: Kopecky, Helmut, Dipl.-Ing. Kopecky & Schwarz Patentanwälte
- 优先权: AT19960001154 19960628
- 国际公布: WO1998002586 19980122
- 主分类号: C21B13
- IPC分类号: C21B13
摘要:
The invention relates to a method for producing liquid pig iron (43) or liquid steel precursors from a hardening material formed by iron ore (5) and additives and having at least partially fines. To achieve a uniform reduction of the iron ore with optimum utilization of the reducing gas, the iron ore (5) is fractionated into at least two fractions, each of them having different grain size distribution, during a first reduction stage (1) with the help of the reducing gas. Each fraction is then reduced with the reducing gas in its own fluidized bed, whereby the reducing gas maintains a first fluidized bed (6) containing the coarse grain fraction and separates the fine grain fraction from it. An additional reducing gas is later introduced directly into the other fluidized bed (15). The reduced iron ore (5) is withdrawn both from the first and from the other fluidized bed (6, 15). The fine and coarse grain fractions reduced during the first reduction stage (1) are further reduced in ore or more additional reduction stages (2) operating in the same way as the first reduction stage (1). The fine grain fraction obtained during the last reduction stage (2) is fed into the smelting-gasification zone (39) under agglomeration by adding oxygen. The coarse grain fraction is gravity fed directly into the smelting-gasification zone (39).
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