The bed voidage, axial dispersion, and kinetic and isotherm parameters for
the chromatographic enantioseparation of racemic Fenoprofen, using cellulos
e ester as the chiral stationary phase and 2-propanol/hexane/acetyl alcohol
as the mobile phase, were evaluated by moment analyses on the basis of equ
ilibrium theory and the linear driving force model. The peak-fitting method
was used to identify the coefficients of the competitive Langmuir isotherm
for both enantiomers. For this reason and for the validation of the model
parameters, a simulation program was developed. The simulated results descr
ibe the experimental data well. On the basis of the isotherm parameters and
the equilibrium theory, the process region for the simulated moving bed (S
MB) process was identified. Changes of the process region will be discussed
by considering fluctuations in the feed concentration and uncertainties in
the determined capacity factor.