A model has been developed for the prediction of multicomponent ion ex
change equilibria which uses equilibrium data from binary systems to p
redict behaviour in multicomponent systems. Non-idealities in the solu
tion phase are considered by applying Pitzer's model for electrolyte b
ehaviour while the resin phase activity coefficients are calculated by
applying Wilson's model. In addition the equilibrium constants are ob
tained from the Gaines and Thomas approach and are independent of the
resin phase activity coefficients. The model also considers the non-av
ailability of some ions for exchange due to the formation of ion pairs
in the solution phase. When applied to cation exchange in the binary
and ternary systems involving H+, Na+, K+ and Ca2+ ions, the model pre
dicts well the equilibrium behaviour. The equilibrium constant and the
two binary interaction parameters are found to be independent of the
conditions of the solution phase including concentration and the parti
cular non-exchanging anionic species present in the solution.