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Equivalent fraction convention, exchanger phase activities

Because the activities of species in the exchanger phase are not well defined in equation 2, a simplified model—that of an ideal mixture—is usually employed to calculate these activities according to the approach introduced bv Vanselow (20). Because of the approximate nature of this assumption and the fact that the mechanisms involved in ion exchange are influenced by factors (such as specific sorption) not represented by an ideal mixture, ion-exchange constants are strongly dependent on solution- and solid-phase characteristics. Thus, they are actually conditional equilibrium constants, more commonly referred to as selectivity coefficients. Both mole and equivalent fractions of cations have been used to represent the activities of species in the exchanger phase. Townsend (21) demonstrated that both the mole and equivalent fraction conventions are thermodynamically valid and that their use leads to solid-phase activity coefficients that differ but are entirely symmetrical and complementary. [Pg.65]

If the equivalent fraction convention for exchanger phase activities is adopted (i.e., the Gaines-Thomas approach), the molar concentrations are proportional to the equivalent fractions, and it can easily be shown that the half reaction constants and the binary-exchange constants (selectivity coefficients) are related by... [Pg.68]


See other pages where Equivalent fraction convention, exchanger phase activities is mentioned: [Pg.110]    [Pg.122]   
See also in sourсe #XX -- [ Pg.68 ]

See also in sourсe #XX -- [ Pg.68 ]




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