4.7 Article

Synergistic separation of Co(II)/Li(I) for the recycling of LIB industry wastes by supported liquid membrane using Cyanex 272 and DR-8R

期刊

HYDROMETALLURGY
卷 101, 期 1-2, 页码 20-27

出版社

ELSEVIER
DOI: 10.1016/j.hydromet.2009.11.012

关键词

Lithium ion battery; Cobalt; Supported liquid membrane; Permeation; Separation; Synergism

资金

  1. Korea Institute of Geosciences and Mineral Resources (KIGAM)
  2. Ministry of Knowledge and Economy of Korea

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The separation of Co(II) and Li(I) from simulated solution of lithium ion battery (LIB) industry wastes has been studied by a supported liquid membrane (SLM) process. The synergistic effect of mixture of the extractants Cyanex 272 and DP-8R on the permeation rate and separation factor of Co(II) and Li(I) from dilute aqueous sulfate media using a supported liquid membrane (SLM) technique has been examined. A microporous hydrophobic PVDF film was used as the solid support for the liquid membrane. The extractants Cyanex 272 and DP-8R and mixture of those were used as mobile carriers. The effects of different parameter such as stirring speed, pH of the feed solution, extractant concentration in the membrane phase. Co(II)/Li(I) concentration in the feed solution, and H2SO4 strip acid concentration, on Co(II) flux (J(co(II))) and Li(I) flux (J(Li(I))) have been studied and compared. For all of the systems studied, Co/Li are optimally separated in the acidic pH region of 5.0-6.0. The best separation factor of 497 was achieved at pH 5.00 using a mixture of Cyanex 272 and DP-8R at a concentration of 750 mol/m(3) in the membrane phase, a strip acid concentration of 100 mol/m(3),and a stirring speed of 350 rpm. The separation factors for all three systems under the respective optimum experimental conditions have been calculated and compared. Qualitatively, they follow the order: mixed-extractant system > Cyanex 272 > DP-8R. This sequence may be quantitatively expressed as: mixed-extractant system approximate to 3 x Cyanex 272 approximate to 15 x DP-8R. (C) 2009 Elsevier B.V. All rights reserved.

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