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METHOD FOR PROCESSING NICKEL LATERITE ORES RESULTING IN THE DIRECT PRODUCTION OF FERRONICKEL

机译:直接生产镍铁的镍红土矿石的加工方法

摘要

The invention relates to the field of non-ferrous metallurgy, and more particularly to a method for processing nickel laterite ores resulting in the direct production of ferronickel in the form of metal granules. Processing nickel laterite ores involves grinding an ore, for example a high-magnesia ore, a solid carbonaceous reducing agent and flux additives, mixing same to produce a charge, subjecting said charge to reduction roasting in a two-stage apparatus consisting of two rotating furnaces interconnected by a transfer chamber, cooling the resulting clinker, and isolating ferronickel from the ground clinker. The flux additives include, in terms of the mass of the ore, 3.5-6.5% СаО, 1.5-10% SiO2, 1-5.5% Al2O3 and 0-0.75%, in terms of F2, fluorine-containing additives. Various calcium-, silicon-, aluminium- and fluorine-containing materials can be used as flux additives, for example limestone, blast furnace slag, clay, low-grade high-silica bauxites, aluminium-containing slags, fluorite, spent cryolite electrolyte, and other enrichment and metal wastes. Kaolin clay containing a minimum of 15-30% Al2O3 and 50-75% SiO2 can be used in an amount of 3-18% of the mass of the ore as SiO2 and Al2O3additives. The solid carbonaceous reducing agent, for example coke breeze, lignite, coal, anthracite or a combination thereof, is introduced in an amount of 6-12% of the mass of the ore, the mixture is briquetted, the briquettes reduced in the first furnace and having a temperature of 1000-1100°C are charged via the transfer chamber into the second furnace, directly into a bath of molten slag. At the same time, a solid reducing agent, namely coke breeze or anthracite, is supplied to the feed zone of the second furnace in an amount of 4-8% of the mass of the ore. The temperature of the melt in the second furnace is maintained within a range of 1275-1350°С, preferably 1275-1325°С. The advantages of the method are reduced energy consumption and improved technical and economic performance indicators.
机译:本发明涉及有色冶金领域,更具体地涉及一种处理镍红土矿石的方法,该方法导致直接生产金属颗粒形式的镍铁。红土镍矿的加工涉及将矿石(例如高镁矿石,固体碳还原剂和助熔剂)研磨,混合以产生炉料,然后在由两个旋转炉组成的两步​​设备中对炉料进行还原焙烧通过传送室相互连接,冷却生成的熟料,并从地面熟料中分离镍铁。按矿石的质量计,助熔剂包括3.5-6.5%СаО,1.5-10%SiO 2 ,1-5.5%Al 2 O 3 和0-0.75%,以F 2 计,是含氟添加剂。各种含钙,硅,铝和氟的材料都可以用作助熔剂添加剂,例如石灰石,高炉矿渣,粘土,低品位高硅铝土矿,含铝矿渣,萤石,废冰晶石电解质,以及其他浓缩和金属废物。可以使用至少3%的Al 2 O 3 和50-75%SiO 2 的高岭土作为SiO 2 和Al 2 O 3 添加剂的矿石质量的-18%。引入固体碳还原剂,例如焦微风,褐煤,煤,无烟煤或它们的组合,其量占矿石质量的6-12%,将混合物压块,并在第一炉中将压块还原温度为1000-1100℃的硅酸盐通过传送室装入第二炉,直接装入熔渣浴中。同时,将固体还原剂即焦风或无烟煤以矿石质量的4-8%的量供应到第二炉的进料区。第二熔炉中的熔体温度保持在1275-1350℃,优选1275-1325℃的范围内。该方法的优点是减少了能源消耗并改善了技术和经济性能指标。

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