TY - JOUR
T1 - Recovery of metals from spent lithium-ion batteries using ionic liquid [P8888][Oleate]
AU - Othman, Enas A.
AU - van der Ham, Aloijsius G.J.
AU - Miedema, Henk
AU - Kersten, Sascha R.A.
N1 - Elsevier deal
PY - 2020/12/1
Y1 - 2020/12/1
N2 - A separation method to selectively recover valuable metals (Co, Ni, Mn and Li) from synthetic spent lithium-ion battery cathodes leachate using a fatty-acid-based ionic liquid, tetraoctylphosphonium oleate [P₈₈₈₈][oleate] is demonstrated. The investigated parameters for this selective separation and recovery process include extraction pH, contact time and composition of the regeneration solution. The benefit of using this ionic liquid is that >99% of Co and >99% of the Mn can be separated from the Ni and the Li by a two-stage extraction process. A subsequent single regeneration process separates the Co from the Mn. Finally, Ni and Li are completely separated in an additional regeneration process. An economic potential analysis concludes the paper, revealing that given the current cobalt price, the process outlined here shows a positive zero-order Economic Potential (bases on product sales and raw material cost) when using a 4 M HCl leaching solution and for leachates containing at least 4.5 g Co per liter.
AB - A separation method to selectively recover valuable metals (Co, Ni, Mn and Li) from synthetic spent lithium-ion battery cathodes leachate using a fatty-acid-based ionic liquid, tetraoctylphosphonium oleate [P₈₈₈₈][oleate] is demonstrated. The investigated parameters for this selective separation and recovery process include extraction pH, contact time and composition of the regeneration solution. The benefit of using this ionic liquid is that >99% of Co and >99% of the Mn can be separated from the Ni and the Li by a two-stage extraction process. A subsequent single regeneration process separates the Co from the Mn. Finally, Ni and Li are completely separated in an additional regeneration process. An economic potential analysis concludes the paper, revealing that given the current cobalt price, the process outlined here shows a positive zero-order Economic Potential (bases on product sales and raw material cost) when using a 4 M HCl leaching solution and for leachates containing at least 4.5 g Co per liter.
KW - UT-Hybrid-D
KW - Lithium-ion battery
KW - Metal recovery
KW - Separation process
KW - Solvent extraction
KW - Ionic liquid
UR - http://www.scopus.com/inward/record.url?scp=85088634770&partnerID=8YFLogxK
U2 - 10.1016/j.seppur.2020.117435
DO - 10.1016/j.seppur.2020.117435
M3 - Article
AN - SCOPUS:85088634770
VL - 252
JO - Separation and purification technology
JF - Separation and purification technology
SN - 1383-5866
M1 - 117435
ER -