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Recovery of Gold and Iron from Cyanide Tailings with a Combined Direct Reduction Roasting and Leaching Process

机译:结合直接还原焙烧和浸出工艺从氰化尾矿中回收金和铁

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Cyanide tailings are the hazardous waste discharged after gold cyanidation leaching. The recovery of gold and iron from cyanide tailings was investigated with a combined direct reduction roasting and leaching process. The effects of reduction temperature, coal dosage and CaO dosage on gold enrichment into Au-Fe alloy (Fe x Au 1?x ) were studied in direct reduction roasting. Gold containing iron powders, i.e., Au-Fe alloy, had the gold grade of 8.23 g/t with a recovery of 97.46%. After separating gold and iron in iron powders with sulfuric acid leaching, ferrous sulfate in the leachate was crystallized to prepare FeSO 4 ·7H 2 O with a yield of 222.42% to cyanide tailings. Gold enriched in acid-leaching residue with gold grade of 216.58 g/t was extracted into pregnant solution. The total gold recovery of the whole process reached as high as 94.23%. The tailings generated in the magnetic separation of roasted products, with a yield of 51.33% to cyanide tailings, had no toxic cyanide any more. The gold enrichment behaviors indicated that higher reduction temperature and larger dosage of coal and CaO could promote the allocation of more gold in iron phase rather than in slag phase. The mechanism for enriching gold from cyanide tailings into iron phase was proposed. This work provided a novel route to simultaneously recover gold and iron from cyanide tailings.
机译:氰化尾矿是金氰化浸出后排放的有害废物。结合直接还原焙烧和浸出工艺,研究了从氰化尾矿中回收金和铁的方法。研究了还原温度,煤添加量和CaO添加量对直接还原焙烧过程中金富集到Au-Fe合金中的影响(Fe x Au 1?x)。含金铁粉即Au-Fe合金的金品位为8.23 g / t,回收率为97.46%。用硫酸浸出法分离铁粉中的金和铁后,将渗滤液中的硫酸亚铁结晶,制得FeSO 4·7H 2 O,氰化尾矿产率为222.42%。将富集了酸浸残渣的金(黄金品位为216.58 g / t)提取到母液中。全过程总金回收率高达94.23%。焙烤产品的磁选中产生的尾渣(氰化物尾渣的收率为51.33%)不再具有有毒的氰化物。金的富集行为表明,较高的还原温度和较大的煤和CaO用量可促进铁相而不是炉渣相中更多的金分配。提出了将氰化物尾矿中的金富集成铁相的机理。这项工作提供了一种从氰化尾矿中同时回收金和铁的新颖途径。

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