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Thermodynamic Modeling of Lithium Extraction from Synthetic Brine Using Deep Eutectic Solvents: A PC-SAFT Approach
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DOI：10.1016/j.fluid.2026.114737.png)
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Abstract
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• Thermodynamic modeling of extraction of lithium from model brine is investigated. • PC-SAFT and ePC-SAFT EOSs are applied to organic and aqueous phases, respectively. • The extractant is a DES comprised of TBAC and DA (1:2) and TOPO as co-extractant. • EOS parameters for DES and TOPO are obtained from density data. • AARD for lithium extraction amount and selectivity over sodium were 7.89 and 8.63.
Keywords:
Lithium extraction
Deep eutectic solvent
PC-SAFT
Thermodynamic modeling
Selectivity
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2.7
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339
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1.5W
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