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Recovery of copper, nickel and cobalt from acidic pressure leaching solutions of low-grade sulfide flotation concentrates

机译:从低品位硫化物浮选精矿的酸性压力浸出溶液中回收铜,镍和钴

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摘要

Recovery of copper, nickel and cobalt from the acidic pressure leaching solutions of Jinbaoshan (YN Province, PRC) low-grade sulfide flotation concentrates was investigated. The proposed technique includes four major steps: (1) the acidity adjustment of the acidic pressure leaching solutions; (2) solvent extraction (SX) separation of copper by organic reagent XD5640, and then stripped from the loaded organic phase by H_2SO_4 solution for copper recovery; then (3) iron in raffinates after copper extracting is selectively removed by high-temperature hydrolysis precipitation in an autoclave; and lastly (4) nickel and cobalt are selectively precipitated by Na_2S from the final solutions after removing iron. The experimental results for treating 1 L acidic leaching solutions per batch by this new technique were reported, and some evaluation and further comparisons with previous investigations were also carried out. It was reported that the total percent recovery of Cu could reach 95 percent or more, and that of Ni and Co were all more than 99 percent. In the processing, the percent removal of impurities, such as Fe, Mg and Ca, were all also near to 99 percent.
机译:研究了金宝山(中国YN省)低品位硫化物浮选精矿的酸性压力浸出溶液中铜,镍和钴的回收率。所提出的技术包括四个主要步骤:(1)调节酸性压力浸出溶液的酸度; (2)用有机试剂XD5640进行溶剂萃取(SX)分离铜,再用H_2SO_4溶液从负载的有机相中汽提,回收铜。然后(3)在高压釜中通过高温水解沉淀选择性地除去提铜后的残液中的铁;最后,在除去铁后,Na_2S从最终溶液中选择性地沉淀出镍和钴(4)。报道了使用该新技术处理每批1 L酸性浸出液的实验结果,并进行了一些评估和进一步的比较。据报道,Cu的总回收率可达到95%或更高,而Ni和Co的总回收率均超过99%。在加工过程中,Fe,Mg和Ca等杂质的去除率也都接近99%。

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