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1 CHEC Research Centre, Department of Chemical and Biochemical Engineering, Technical University of Denmark 2 Department of Chemical and Biochemical Engineering, Technical University of Denmark 3 Department of Applied Chemistry, Technical University of Denmark 4 unknown
The experimental realization of a continuous preferential crystallization process, consisting of two mixed-flow crystallizers coupled via crystal-free liquid exchange streams and with only the liquid phases operating continuously, is addressed. Experiments in triplicate, using the conglomerate-forming system of dl-asparagine monohydrate in water, were conducted, and the achievement of nearly racemic composition of the liquid phase in the crystallizers was verified. An experiment was also carried out using seed crystals of a smaller average particle size than used in the reference experiments. Successful enantioseparation by crystal growth, with the repeatability being within ±10% deviation, was obtained. However, slow crystal growth, due to a low surface integration rate, led to a negligible consumption of the desired enantiomer added in the feed solution, resulting in low productivities. Productivities, yields, and purities of solid products were influenced by the morphological differences in the seed crystals. Due to irregularly shaped seed crystals, increase in the productivities and yields were achieved in the L-Tank. Lower purities of solid products from the L-Tank compared to purities of the solid products from the D-Tank were obtained. This could be due to surface nucleation of d-asparagine monohydrate, ascribed to the surface structure of the seeds of l-asparagine monohydrate supplied. Improvements in productivity, yield, and purity in the L-Tank, for the same process duration, were realized using seed crystals of lower average particle size having a smoother surface structure. The main advantages compared to other separation processes are low capital cost, high crystal purity and yield, ease of upscaling, increased safety, and reduced environmental impact due to reduction in the amount of solvent used. The application is currently limited to conglomerate-forming systems, but the separation concept may open new possibilities for process improvements regarding enantioseparation of racemic compound-forming systems as well. © 2013 American Chemical Society.
Organic Process Research and Development, 2013, Vol 17, Issue 8, p. 1010-1020
Amino acids; Crystal growth; Enantiomers; Environmental impact; Experiments; Liquids; Particle size; Productivity; Surface structure; Tanks (containers); Crystallizers
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