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Bioleaching strategies for the treatment of nickel-copper sulphide concentrates

机译:生物浸出法处理硫化镍铜精矿

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摘要

Different process options for the bioleaching of nickel-copper containing sulphide concentrates were evaluated. Tests in continuously operated reactor systems showed >98% nickel extractions over a range of temperatures, whereas for copper occurring as chalcopyrite, extractions of >95% could only be achieved at 70 °C. During further optimisation of the process the effects of process parameters such as grind size, residence time, redox potential and feed solids concentration on the leach kinetics, metal extractions and performance of both moderate thermophile and thermophile cultures were addressed. Redox control in the first-stage reactor of thermophilic systems resulted in considerably faster copper leach rates and extractions of up to 95% could be achieved at increased feed concentrations and coarser grind sizes. High redox levels in the secondary reactors ensured >98% nickel recoveries. These operating conditions and control strategies have the potential to increase the rates of nickel and copper extractions to the extent that leaching times could be considerably reduced.
机译:评估了生物浸出含镍铜硫化物精矿的不同工艺选择。在连续运行的反应器系统中进行的测试表明,在一定温度范围内,镍的提取率> 98%,而对于黄铜矿中的铜,只有在70°C时才能提取> 95%。在进一步优化工艺过程中,研究了工艺参数(如磨料大小,停留时间,氧化还原电势和进料固体浓度)对浸出动力学,金属萃取和中性嗜热和嗜热培养物性能的影响。嗜热系统第一阶段反应器中的氧化还原控制可显着加快铜的浸出速度,在进料浓度提高和研磨粒度更大的情况下,提取率最高可达到95%。二级反应器中高的氧化还原水平确保了> 98%的镍回收率。这些操作条件和控制策略有可能将镍和铜的提取率提高到一定程度,从而可以大大减少浸出时间。

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