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DOI: 10.1039/A902669J (Paper) Reference Section for: J. Chem. Res. (S), 1999, 518-519

Solvent Extraction Equilibrium in the CuSO4–H2SO4–LIX 984–ESCAID 103 System

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Francisco José Alguacil, Jaime Simpson and Patricio Navarro

Abstract

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.

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