Research on the short-process of leaching and semi-extraction method of nickel‑cobalt from mixed hydroxide precipitate (MHP) to prepare battery grade products

IF 4.8 2区 材料科学 Q1 METALLURGY & METALLURGICAL ENGINEERING
Yukun Shen , Hongyu Wang , Liang Zhang , Liyong Zhou , Chunping Fu , Kweon Ho Jin , Mingkang Fang , Jiade Wang
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Abstract

Mixed nickel‑cobalt hydroxide precipitate (MHP) obtained via pretreatment and leaching of nickel laterite ore, is a vital source of nickel and cobalt. This work proposes an efficient and economical hydrometallurgical process for recovering Ni and Co from MHP. Initially, an acid leaching process was employed, achieving leaching efficiencies of 99.9 % for Ni and 98.3 % for Co. Notably, the leaching efficiency for Mn was significantly lower at 26.1 %, attributed to partial oxidation of Mn. Subsequently, the purification of the leach liquor resulted in a significant reduction of impurities such as Si, Sc, Fe, and Al to concentrations of 18 mg/L, 1.8 mg/L, 0.8 mg/L, and 0.8 mg/L, respectively. Finally, the subsequent semi-extraction process further minimized impurities, including Co, Mn, Mg, and Ca, to levels below 1 mg/L in the purified solution. Furthermore, the Sc enriched in P204 was stripped by 3 mol/L NaOH, yielding a Sc-enriched solid residue with a grade of 30 %. The results show that the process can extract Ni and Co from MHP, and Ni, Co solution are suitable for the production of lithium batteries.
从混合氢氧化物(MHP)中浸出镍钴半萃取制备电池级产品的短工艺研究
红土镍矿经预处理和浸出得到的混合镍钴氢氧化物沉淀(MHP)是镍和钴的重要来源。本工作提出了一种高效、经济的湿法冶金从MHP中回收Ni和Co的工艺。最初,采用酸浸工艺,镍的浸出效率为99.9%,钴的浸出效率为98.3%。值得注意的是,锰的浸出效率明显较低,为26.1%,这是由于锰的部分氧化。随后,对浸出液进行提纯,使Si、Sc、Fe和Al等杂质的浓度分别显著降低至18mg /L、1.8 mg/L、0.8 mg/L和0.8 mg/L。最后,随后的半萃取过程进一步减少杂质,包括Co, Mn, Mg和Ca,纯化溶液中的含量低于1mg /L。此外,用3 mol/L NaOH对P204中富集的Sc进行剥离,得到品位为30%的富Sc固体残渣。结果表明,该工艺可以从MHP中提取出Ni和Co,且Ni、Co溶液适合生产锂电池。
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来源期刊
Hydrometallurgy
Hydrometallurgy 工程技术-冶金工程
CiteScore
9.50
自引率
6.40%
发文量
144
审稿时长
3.4 months
期刊介绍: Hydrometallurgy aims to compile studies on novel processes, process design, chemistry, modelling, control, economics and interfaces between unit operations, and to provide a forum for discussions on case histories and operational difficulties. Topics covered include: leaching of metal values by chemical reagents or bacterial action at ambient or elevated pressures and temperatures; separation of solids from leach liquors; removal of impurities and recovery of metal values by precipitation, ion exchange, solvent extraction, gaseous reduction, cementation, electro-winning and electro-refining; pre-treatment of ores by roasting or chemical treatments such as halogenation or reduction; recycling of reagents and treatment of effluents.
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