The paper deals with chiral separation by simulated moving bed (SMB) chroma
tography. A model for the prediction of the cyclic steady-state performance
of the SMB, based on the analogy with the true moving bed (TMB), is develo
ped assuming multicomponent adsorption equilibria, axial dispersion flow an
d the linear driving force approximation to describe the intraparticle mass
transfer rate. The simulation package is used to predict the effect of ope
rating variables on the process performance and to define the regions for e
nantiomers separation. The influence of mass transfer resistance in the sep
aration region is analyzed. A practical tool for choosing the better SMB op
erating conditions as a function of the feed flow-rate is proposed. The exp
erimental operation of a pilot unit of SMB, Licosep 12-26 (Novasep, France)
, is carried out for the separation of enantiomers and illustrated with two
systems: the bi-naphthol and the chiral epoxide enantiomers. Experimental
results and model predictions are compared in terms of process performance
and internal concentration profiles. (C) 2000 Elsevier Science B.V. All rig
hts reserved.