ABSTRACT
The simulated moving bed (SMB) technology offers the possibility of scaling up single column, batch chromatographic separations to continuous operation. This has proved particularly effective for the separation of enantiomers, and has been applied in the liquid and gas phase, as well as using a supercritical fluid as eluent (SF-SMB). In the last case, the main performance improvements are due to the possibility of tuning the elution strength of the mobile phase, by changing the pressure in the four sections of the SMB unit. Thus a SF-SMB can be operated in two modes, i.e. the isocratic and the pressure gradient mode. In this research, design criteria for these two operating modes have been developed, which can be applied to systems described by linear as well as nonlinear Langmuir adsorption isotherms. The role and effect of an appropriate modifier in increasing solubility and reducing retention times have been investigated. The results reported allow to identify the operating conditions, including the pressure levels and the modifier concentration, which lead to optimal separation performance in terms of productivity and desorbent requirement.
