A statistical mechanical lattice model of a reactive solvent extractio
n process involving two phase liquid-liquid ion exchange is presented.
It is applied to literature data on the extraction of aliphatic carbo
xylic acids by quaternary ammonium salts. The Helmholtz free energy of
the system is constructed and minimised subject to the constraints of
mass balance and electroneutrality. The equations defining the equili
brium conditions have been solved numerically for a range of interacti
on parameters and hence the equilibrium concentrations of the various
partitioned species are obtained. These interaction parameters are com
pared with experiment. The intuitive notion that the extent of partiti
on is dominated by electrostatic solute-extractant interactions is sho
wn to neglect various other interactions that may, in some systems, be
important. (C) 1997 Elsevier Science B.V.