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Enabling mechanical separation of enantiomers through controlled batchwise concomitant crystallization: digital design and experimental validation

Andrew S. Dunn, Botond Szilagyi, Joop H. ter Horst*, Zoltan K. Nagy

*Corresponding author for this work

Research output: Contribution to journalArticlepeer-review

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Abstract

In the pharmaceutical industry the separation of chiral molecules is important due to the different physiochemical properties that the enantiomers of a chiral drug possess. Therefore, resolution techniques are used to separate such enantiomers from one another. In particular, preferential crystallization is a common technique used to separate conglomerate-forming compounds, due to its high selectivity. However, the efficient separation of enantiomers in a batchwise preferential crystallization process through seeding with the preferred enantiomer alone is still inefficient, since unwanted nucleation of the counter enantiomer is inevitable. Here, we demonstrate a model-based digital design for the separation of enantiomers for a conglomerate-forming compound (asparagine monohydrate), by using mechanical separation by sieving after crystallization, whereby the separation is enabled by a designed bias in the crystal size distributions of each enantiomer. This bias is created by a concomitant crystallization of both enantiomers using optimized seeding and cooling profiles obtained from a population balance model. In this way, a high level of control is achieved over a batchwise preferential crystallization process, since the crystallization of both enantiomers is controlled. We show that, through this separation method, material with impurity levels as low as 6 wt % can be obtained. To our knowledge this is the first demonstration of modeling such a process to separate enantiomers of a conglomerate-forming compound.

Original languageEnglish
Pages (from-to)7726-7741
Number of pages16
JournalCrystal Growth and Design
Volume20
Issue number12
Early online date28 Oct 2020
DOIs
Publication statusPublished - 2 Dec 2020

Funding

A.S.D. thanks the Nagy group at Purdue Univeristy, Indiana, for the hospitality that he enjoyed during his three-month research visit on the topic of this paper. We thank the EPSRC and the Doctoral Training Centre in Continuous Manufacturing and Crystallization (Grant No. EP/K503289/1) for funding this work. The authors acknowledge that the experimental work was performed in the CMAC National Facility supported by UKRPIF (UK Research Partnership Fund) award from the Higher Education Funding Council for England (HEFCE) (Grant No. HH13054). The authors also acknowledge the International Fine Particles Research Institute (IFPRI) for partial financial support (Grant No. FRR-21-09).

Keywords

  • preferential crystallization
  • mechanical separation
  • concomitant crystallization
  • digital design of crystallization
  • crystallization control
  • enantioseparation
  • asparagine monohydrate

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