A previously determined thermodynamic model for extraction equilibrium is used as a basis to predict experimentally measured distribution coefficients for the CuSO4–H2SO4–LIX 984–Escaid 103 solvent extraction system at 25°C and aqueous copper concentrations in the range 0.01–2.0 g L–1, the copper loading isotherm is also obtained.
F. José Alguacil, J. Simpson and P. Navarro, J. Chem. Res. (S), 1999, 518 DOI: 10.1039/A902669J
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