Abstract
A Couette cell flow device was designed, and an experimental procedure was developed to enable a quantitative study of the effects of fluid shear on secondary nucleation using a fixed seed crystal under controlled supersaturation, temperature, and flow conditions. This approach excludes mechanical impact, which is often considered to be the principal source of secondary nucleation, for example, through crystal attrition. We found that secondary nucleation rates of α-glycine in aqueous solutions induced by fluid shear were very significant and about 6 orders of magnitude higher than primary nucleation rates at the same conditions. Secondary nucleation rates per seed crystal were found to be about 1 order of magnitude lower compared with the magnetically stirred vials investigated previously, where a single seed crystal was freely moving, and thus, its mechanical impacts could not be ruled out. Computational fluid dynamics was used to calculate the wall shear stress along the surface of fixed seed crystals placed in the Couette cell gap at rotation rates between 100 and 600 rpm investigated here. This approach allows relating the secondary nucleation rate to the wall shear stress so that quantitative models can be developed to capture the effects of fluid shear on secondary nucleation kinetics. Such models will then facilitate scale-up and transfer of secondary nucleation kinetics between various equipment used in industrial crystallization processes.
Original language | English |
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Pages (from-to) | 4975-4984 |
Number of pages | 10 |
Journal | Crystal Growth and Design |
Volume | 24 |
Issue number | 12 |
Early online date | 10 Jun 2024 |
DOIs | |
Publication status | Published - 19 Jun 2024 |
Funding
The authors would like to acknowledge that this work was carried out in the CMAC National Facility housed within the University of Strathclyde’s Technology Innovation Centre and funded with a UKRPIF (UK Research Partnership Institute Fund) capital award (Grant Ref: HH13054) from the Higher Education Funding Council for England (HEFCE). We would like to acknowledge funding from EPSRC Continuous Manufacturing and Advanced Crystallisation Future Manufacturing Research Hub (Grant reference: EP/P006965/1) and from GSK.
Keywords
- Couette cell flow device
- fluid shear
- secondary nucleation
- α-glycine
- crystallisation processes