Kinetically controlled preferential crystallization (PC) is a well-established elegant concept to separate mixtures of enantiomers of conglomerate-forming systems. Based on a smaller number of laboratory investigations, the key parameters of an available shortcut model (SCM) can be estimated, allowing for a rapid and reliable process design. This paper addresses a severe limitation of the method, namely, the limitation of the yield to 50%. In order to exploit the valuable counter enantiomer, the crystallization process is studied, coupled with a racemization reaction and a recycling step. It will be shown that the process integration can be performed in various ways. To quantify the different options in a unified manner and to provide a more general design concept, the SCM of PC is extended to include a kinetic model for the enzymatically catalyzed reaction. For illustration, model parameters are used, which characterize the resolution of the enantiomers of asparagine monohydrate and the racemization rate using an amino acid racemase. The theoretical study highlights the importance of exploiting the best stop time for batch operations in order to achieve the highest process productivity.
© 2022 The Authors. Published by American Chemical Society.