High-Performance Recovery of Cobalt and Nickel from the Cathode Materials of NMC Type Li-Ion Battery by Complexation-Assisted Solvent Extraction

The annual global volume of waste lithium-ion batteries (LIBs) has been increasing over years. Although solvent extraction method seems well developed, the separation factor between cobalt and nickel is still relatively low—only 72 when applying conventional continuous-countercurrent extraction. In...

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Main Authors: Wen-Yu Wang, Hong-Chi Yang, Ren-Bin Xu
Format: Article
Language:English
Published: MDPI AG 2020-07-01
Series:Minerals
Subjects:
Online Access:https://www.mdpi.com/2075-163X/10/8/662
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spelling doaj-3542acee732a4e2da2d1ac8b1808e0532020-11-25T03:22:50ZengMDPI AGMinerals2075-163X2020-07-011066266210.3390/min10080662High-Performance Recovery of Cobalt and Nickel from the Cathode Materials of NMC Type Li-Ion Battery by Complexation-Assisted Solvent ExtractionWen-Yu Wang0Hong-Chi Yang1Ren-Bin Xu2Department of Environmental Engineering and Management, Chaoyang University of Technology, Taichung 41349, TaiwanDepartment of Environmental Engineering and Management, Chaoyang University of Technology, Taichung 41349, TaiwanDepartment of Environmental Engineering and Management, Chaoyang University of Technology, Taichung 41349, TaiwanThe annual global volume of waste lithium-ion batteries (LIBs) has been increasing over years. Although solvent extraction method seems well developed, the separation factor between cobalt and nickel is still relatively low—only 72 when applying conventional continuous-countercurrent extraction. In this study, we improved the separation factor of cobalt and nickel by complexation-assisted solvent extraction. Before solvent extraction procedure, leaching kinetic of Li, Ni, Co and Mn was studied and can be explained by the Avrami equation. Leached residues were also investigated by SEM and XRD. Operation parameters of complexation-assisted solvent extraction were examined, including volume ratio of extractant to diluent, types of diluent, type of complexing reagent, extractant saponification percentage and volume ratio of organic phase to aqueous phase. The optimal separation factor of complexation-assisted solvent extraction could be improved to 372, which is five times that of conventional solvent extraction. The separation tendency would be interpreted by the relationship between extraction equilibrium pH and log distribution coefficient.https://www.mdpi.com/2075-163X/10/8/662recycling lithium-ion batteriessolvent extractioncomplexing reactioncobaltnickel
collection DOAJ
language English
format Article
sources DOAJ
author Wen-Yu Wang
Hong-Chi Yang
Ren-Bin Xu
spellingShingle Wen-Yu Wang
Hong-Chi Yang
Ren-Bin Xu
High-Performance Recovery of Cobalt and Nickel from the Cathode Materials of NMC Type Li-Ion Battery by Complexation-Assisted Solvent Extraction
Minerals
recycling lithium-ion batteries
solvent extraction
complexing reaction
cobalt
nickel
author_facet Wen-Yu Wang
Hong-Chi Yang
Ren-Bin Xu
author_sort Wen-Yu Wang
title High-Performance Recovery of Cobalt and Nickel from the Cathode Materials of NMC Type Li-Ion Battery by Complexation-Assisted Solvent Extraction
title_short High-Performance Recovery of Cobalt and Nickel from the Cathode Materials of NMC Type Li-Ion Battery by Complexation-Assisted Solvent Extraction
title_full High-Performance Recovery of Cobalt and Nickel from the Cathode Materials of NMC Type Li-Ion Battery by Complexation-Assisted Solvent Extraction
title_fullStr High-Performance Recovery of Cobalt and Nickel from the Cathode Materials of NMC Type Li-Ion Battery by Complexation-Assisted Solvent Extraction
title_full_unstemmed High-Performance Recovery of Cobalt and Nickel from the Cathode Materials of NMC Type Li-Ion Battery by Complexation-Assisted Solvent Extraction
title_sort high-performance recovery of cobalt and nickel from the cathode materials of nmc type li-ion battery by complexation-assisted solvent extraction
publisher MDPI AG
series Minerals
issn 2075-163X
publishDate 2020-07-01
description The annual global volume of waste lithium-ion batteries (LIBs) has been increasing over years. Although solvent extraction method seems well developed, the separation factor between cobalt and nickel is still relatively low—only 72 when applying conventional continuous-countercurrent extraction. In this study, we improved the separation factor of cobalt and nickel by complexation-assisted solvent extraction. Before solvent extraction procedure, leaching kinetic of Li, Ni, Co and Mn was studied and can be explained by the Avrami equation. Leached residues were also investigated by SEM and XRD. Operation parameters of complexation-assisted solvent extraction were examined, including volume ratio of extractant to diluent, types of diluent, type of complexing reagent, extractant saponification percentage and volume ratio of organic phase to aqueous phase. The optimal separation factor of complexation-assisted solvent extraction could be improved to 372, which is five times that of conventional solvent extraction. The separation tendency would be interpreted by the relationship between extraction equilibrium pH and log distribution coefficient.
topic recycling lithium-ion batteries
solvent extraction
complexing reaction
cobalt
nickel
url https://www.mdpi.com/2075-163X/10/8/662
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