Lithium extraction from salt lake via rocking-chair flow electrode capacitive deionization with monovalent selective membrane
This work developed a novel rocking-chair flow electrode capacitive deionization (R-FCDI) system that employs the commercial monovalent selective membrane (CMSM) to realize extremely efficacious separation of Li+/Mg2+ ions with extracting lithium from salt lake brine. The R-FCDI system exhibits exce...
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Veröffentlicht in: | Desalination 2025-05, Vol.600, p.118516, Article 118516 |
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Zusammenfassung: | This work developed a novel rocking-chair flow electrode capacitive deionization (R-FCDI) system that employs the commercial monovalent selective membrane (CMSM) to realize extremely efficacious separation of Li+/Mg2+ ions with extracting lithium from salt lake brine. The R-FCDI system exhibits exceptional lithium extraction performance, obtaining an electrosorption efficiency (ESR) of 98.4 %, an average electrosorption rate (AESR) of up to 7.77 μmol cm−2 min−1, a high charge efficiency (CE) of 93.44 %, and energy consumption (Em) as low as 0.07 kWh mol−1 Li. Especially, the Em is considerably lower than that of electrodialysis (ED, 0.13–3.795 kWh mol−1 Li), making it a suitable option for industrial lithium extraction by reducing the operational costs. Moreover, the selectivity coefficient of the system reached a maximum value of 15.93 with low Em (0.037 kWh mol−1 Li) when the magnesium/lithium mass ratio was 10 under a low applied voltage of 0.8 V. The electrochemical measurements reveal that the selective mechanism of Li+/Mg2+ ion in the proposed R-FCDI system is ascribed to the significantly higher capacitance of lithium ions (1.13-fold as greater as that of magnesium ions) and the substantially lower transmembrane transfer resistance of lithium ions (2.48-fold lower compared to that of magnesium ions). Interestingly, this study found that the initial ion concentration of the recovered solution has a marked consequence on the selectivity coefficient of the R-FCDI system, in which the highest selectivity coefficient of 34.99 with low Em (0.042 kWh mol−1 Li) was achieved when the ion concentration is 500 mg L−1. In an experimental study of the natural brine from Golmud salt lake, China, the maximum of selectivity coefficient is 24.74 and the Em is 3.03 kWh mol−1 Li at optimal process parameters.
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•R-FCDI system integrates feed and recovery channels utilizing a monovalent selective membrane.•R-FCDI has high extraction efficiency, electrosorption rate, and low molar energy consumption.•The initial ion concentrations in recovered solution impacted separation coefficient of R-FCDI.•The R-FCDI achieved a maximum selectivity coefficient of 15.93 when the Mg2+/Li+ mass ratio was 10.•The excellent lithium extraction performance of R-FCDI was verified in natural salt lake brine. |
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ISSN: | 0011-9164 |
DOI: | 10.1016/j.desal.2024.118516 |