| 摘要 |
<p>A method and apparatus for the direct reduction of iron ore are disclosed. A mixture of iron ore, solid carbonaceous fuel and, if sulfur is present, calcined limestone or dolomite, are used. The carbonaceous material can be cellulosic material (wood waste, paper, particularly municipal trash, garbage, etc.), charcoal, or coal (preferably sub-bituminous coal or lignite). The above feed is continuously charged into a gasification and initial reduction zone of a shaft furnace which is partitioned partially from the remainder of the furnace. Oxygen and hot steam are introduced into the upper portion of the said zone. Partial combustion or pyrolysis of the fuel and reaction with steam take place, producing reducing gas which initiates reduction of the iron ore. Ore and gas flow downwardly through conduits into the final reduction zone. Meanwhile, hydrogen-enriched reducing gas is introduced in the middle of the final reduction zone. Top gas is withdrawn from the upper open space of the final reduction zone, drawing reducing gas downwardly from the gasification and initial reduction zone and upwardly through the final reduction zone. In addition, top gas is withdrawn from the bottom of the final reduction zone. Reduction of the iron ore to sponge iron is completed in the final reduction zone. A portion of the withdrawn top gas is cooled, purified of dust, carbon dioxide and sulfur and dehumidified, then introduced near the bottom of the shaft furnace. It ascends, cooling and carburizing the sponge iron descending from the final reduction zone and becoming heated. The cooling gas is then withdrawn from the bottom of the final reduction zone. A special form of discharge grate discharges iron successively from different areas, so as to produce agitation and mixing.</p> |
