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
{"title":"Research on the short-process of leaching and semi-extraction method of nickel‑cobalt from mixed hydroxide precipitate (MHP) to prepare battery grade products","authors":"Yukun Shen , Hongyu Wang , Liang Zhang , Liyong Zhou , Chunping Fu , Kweon Ho Jin , Mingkang Fang , Jiade Wang","doi":"10.1016/j.hydromet.2025.106446","DOIUrl":null,"url":null,"abstract":"<div><div>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.</div></div>","PeriodicalId":13193,"journal":{"name":"Hydrometallurgy","volume":"233 ","pages":"Article 106446"},"PeriodicalIF":4.8000,"publicationDate":"2025-01-29","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Hydrometallurgy","FirstCategoryId":"88","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0304386X25000118","RegionNum":2,"RegionCategory":"材料科学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"METALLURGY & METALLURGICAL ENGINEERING","Score":null,"Total":0}
引用次数: 0
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.
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.