A cleaner and sustainable method for recovering rare earth and cobalt from NdFeB leaching residues

被引:13
作者
Zhang, Liping [1 ,3 ]
Xiao, Wanhai [1 ]
Li, Guobiao [1 ]
Wang, Dong [1 ,2 ,5 ,6 ]
Wu, Jian [1 ,2 ,4 ]
Du, Haojie [2 ]
Lin, Yong [1 ]
Ye, Chunlin [4 ]
Qi, Tao [1 ]
Wang, Zhi [2 ,5 ,6 ]
机构
[1] Chinese Acad Sci, Ganjiang Innovat Acad, Jiangxi Prov Key Lab Cleaner Prod Rare Earths, Ganzhou 341119, Peoples R China
[2] Chinese Acad Sci, Inst Proc Engn, Natl Engn Res Ctr Green Recycling Strateg Met Reso, Key Lab Green Proc & Engn, Beijing 100190, Peoples R China
[3] Nanchang Univ, Nanchang 330031, Peoples R China
[4] China Rare Earth Grp Co Ltd, Ganzhou 341000, Peoples R China
[5] Chinese Acad Sci, Innovat Acad Green Manufacture, Beijing 100190, Peoples R China
[6] 1 BeiErJie, Beijing 100190, Peoples R China
关键词
NdFeB leaching residues; Reductive acid leaching; REEs; Cobalt; Recycling; TRANSITION-METALS; VALUABLE METALS; SULFURIC-ACID; ELEMENTS; MAGNETS; SEPARATION; EXTRACTION; BATTERIES;
D O I
10.1016/j.jclepro.2023.138576
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
NdFeB leaching residues (NLRs) is produced by the treatment of NdFeB waste by HCl preferential dissolution method, which contains about 1% rare earth and cobalt (Co). The extraction of valuable elements from the residue has a great impact on the sustainable utilization of rare-earth resources. In this study, a high-efficiency hydrometallurgy process was proposed to achieve a high conversion of valuable elements and the recycling of additives by reductive acid leaching. First, NLRs were characterized by the Bgrimm process mineralogy analyzing system, which confirmed that the iron oxide main phase encapsulates the rare earth phase. It was effective in destroying the main phase by chemical dissociation. In addition, the effects of temperature, reaction time, initial acid concentration, solid-liquid ratio (S/L), and reducing agent dosage on leaching efficiency were investigated. Under optimal conditions, 90.6% Co, 89.1% neodymium (Nd), 77.2% praseodymium (Pr), 88.7% cerium (Ce) and 83.8% iron (Fe) leached. The reaction mechanism and leaching kinetics in the leaching process were systematically explored. The kinetic analysis indicated the leaching reaction of Co and Fe was controlled by interfacial chemical reaction and the leaching reaction of Nd, Pr and Ce was controlled by internal diffusion. The activation energies of Co, Fe, Nd, Pr and Ce were 21.06, 18.07, 23.37, 20.56 and 18.52 kJ/mol. Furthermore, the reducing agent (copper powder) was successfully recovered by iron powder. The recovery rate of the copper powder was 99.93% and the purity was 93.42%. The proposed process has a promising application for industrialscale recycling.
引用
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页数:11
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