Separation of cobalt, nickel, and copper metal using the mixture of HCl in ethylene glycol and Aliquat 336 in kerosene

The recovery of valuable metals such as Co, Cu, and Ni from spent lithium-ion batteries has attracted much attention due to environmental issues and economic values. Separation of these metals from the synthetic metallic mixtures was investigated by employing nonaqeous solvent. In this work, the mix...

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Main Authors: Thanh Tuan Tran, Yang Liu, Man Seung Lee
Format: Article
Language:English
Published: Elsevier 2021-09-01
Series:Journal of Materials Research and Technology
Subjects:
Online Access:http://www.sciencedirect.com/science/article/pii/S2238785421008024
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spelling doaj-e327328c424d4d2baa07d72e125e2f2a2021-09-25T05:07:28ZengElsevierJournal of Materials Research and Technology2238-78542021-09-011423332344Separation of cobalt, nickel, and copper metal using the mixture of HCl in ethylene glycol and Aliquat 336 in keroseneThanh Tuan Tran0Yang Liu1Man Seung Lee2Department of Advanced Materials Science & Engineering, Institute of Rare Metal, Mokpo National University, Chonnam, 534-729, Republic of KoreaCollege of Environment and Safety Engineering, Qingdao University of Science and Technology, 53 Zhengzhou Road, Qingdao, 266042, ChinaDepartment of Advanced Materials Science & Engineering, Institute of Rare Metal, Mokpo National University, Chonnam, 534-729, Republic of Korea; Corresponding author.The recovery of valuable metals such as Co, Cu, and Ni from spent lithium-ion batteries has attracted much attention due to environmental issues and economic values. Separation of these metals from the synthetic metallic mixtures was investigated by employing nonaqeous solvent. In this work, the mixture of HCl in ethylene glycol (EG) and Aliquat 336 in kerosene was employed as nonaqeous solvents and the leaching conditions were optimized. Under the optimum condition, Ni was completely leached and remained in the EG phase with 99.8% purity. Meanwhile, the leaching percentage of Co(II) and Cu(II) was 62.3% and 18.3% and most of the two dissolved metal ions were extracted into Aliquat 336 phase. After complete stripping of Co(II) and Cu(II) from the loaded Aliquat 336 phase with 2.0 mol L−1 H2SO4, Cu(II) was selectively extracted over Co(II) by 0.1 mol L−1 Cynanex301 and then stripped by 50% aqua regia solution with >99.9% purity. The purity of Co(II) in the raffinate was 99.6%. Besides, Co from the leaching residue was selectively dissolved over Cu by 5.0 mol L−1 H2SO4 with 99.6% purity. A process was proposed for the separation of Co, Cu and Ni from metallic mixtures. The process showed some advantages in terms of the high purity of the metal solutions recovered and a decrease in the number of steps for the metal recovery. Thus, the application of this process to real operation can be considered.http://www.sciencedirect.com/science/article/pii/S2238785421008024Non-aqueous leachingCobaltNickelAlloysLithium-ion battery
collection DOAJ
language English
format Article
sources DOAJ
author Thanh Tuan Tran
Yang Liu
Man Seung Lee
spellingShingle Thanh Tuan Tran
Yang Liu
Man Seung Lee
Separation of cobalt, nickel, and copper metal using the mixture of HCl in ethylene glycol and Aliquat 336 in kerosene
Journal of Materials Research and Technology
Non-aqueous leaching
Cobalt
Nickel
Alloys
Lithium-ion battery
author_facet Thanh Tuan Tran
Yang Liu
Man Seung Lee
author_sort Thanh Tuan Tran
title Separation of cobalt, nickel, and copper metal using the mixture of HCl in ethylene glycol and Aliquat 336 in kerosene
title_short Separation of cobalt, nickel, and copper metal using the mixture of HCl in ethylene glycol and Aliquat 336 in kerosene
title_full Separation of cobalt, nickel, and copper metal using the mixture of HCl in ethylene glycol and Aliquat 336 in kerosene
title_fullStr Separation of cobalt, nickel, and copper metal using the mixture of HCl in ethylene glycol and Aliquat 336 in kerosene
title_full_unstemmed Separation of cobalt, nickel, and copper metal using the mixture of HCl in ethylene glycol and Aliquat 336 in kerosene
title_sort separation of cobalt, nickel, and copper metal using the mixture of hcl in ethylene glycol and aliquat 336 in kerosene
publisher Elsevier
series Journal of Materials Research and Technology
issn 2238-7854
publishDate 2021-09-01
description The recovery of valuable metals such as Co, Cu, and Ni from spent lithium-ion batteries has attracted much attention due to environmental issues and economic values. Separation of these metals from the synthetic metallic mixtures was investigated by employing nonaqeous solvent. In this work, the mixture of HCl in ethylene glycol (EG) and Aliquat 336 in kerosene was employed as nonaqeous solvents and the leaching conditions were optimized. Under the optimum condition, Ni was completely leached and remained in the EG phase with 99.8% purity. Meanwhile, the leaching percentage of Co(II) and Cu(II) was 62.3% and 18.3% and most of the two dissolved metal ions were extracted into Aliquat 336 phase. After complete stripping of Co(II) and Cu(II) from the loaded Aliquat 336 phase with 2.0 mol L−1 H2SO4, Cu(II) was selectively extracted over Co(II) by 0.1 mol L−1 Cynanex301 and then stripped by 50% aqua regia solution with >99.9% purity. The purity of Co(II) in the raffinate was 99.6%. Besides, Co from the leaching residue was selectively dissolved over Cu by 5.0 mol L−1 H2SO4 with 99.6% purity. A process was proposed for the separation of Co, Cu and Ni from metallic mixtures. The process showed some advantages in terms of the high purity of the metal solutions recovered and a decrease in the number of steps for the metal recovery. Thus, the application of this process to real operation can be considered.
topic Non-aqueous leaching
Cobalt
Nickel
Alloys
Lithium-ion battery
url http://www.sciencedirect.com/science/article/pii/S2238785421008024
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