A mathematical model is presented to simulate Cs exchange in fixed-bed colu
mns of a novel crystalline silicotitanate (CST) material, UOP IONSIV IE-911
. A local equilibrium is assumed between the macropores and the solid cryst
als for the particle material balance. Axial dispersed flow and film mass-t
ransfer resistance are incorporated into the column model. Cs equilibrium i
sotherms and diffusion coefficients were measured experimentally, and dispe
rsion and film mass-transfer coefficients were estimated from correlations.
Cs exchange column experiments were conducted in 5-5.7 M Na solutions and
simulated using the proposed model. Best-fit diffusion coefficients from co
lumn simulations were compared with previously reported batch values of Gu
et al. and Huckman. Cs diffusion coefficients for the column were between 2
.5 and 5.0 x 10(-11) m(2)/s for 5-5.7 M Na solutions. The effect of the iso
therm shape on the Cs diffusion coefficient was investigated. The proposed
model provides good fits to experimental data and may be utilized in design
ing commercial-scale units.