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- 2012 AIChE Annual Meeting
- Separations Division
- Nucleation and Growth II
- (514d) Simulation of the Crystal Shape Distribution in the Presence of Growth Modifiers
In this work, we present a modelling framework and simulation results that can be used to predict the evolution of crystal shape distribution in a crystallizer in the presence of GM. The growth rate of the crystals depends not only on the concentration of the GM, but also the time during which the crystals are exposed to the GM in the mother liquor [5]. These two aspects have recently been incorporated in a mono-dimensional PBM proposed by Fevotte and Fevotte [4]. We further extend this model to a multi-dimensional PBM so that morphological PBM describing the evolution of crystal shape distribution can also be incorporated.
Following the model by Kubota and Mullin [6], the growth rate dependence on the GM concentration is described by surface coverage of the adsorbed species on the growing crystal and a proportionality constant denoting the effectiveness of the adsorbed species. On the other hand, in order to track the contact time of the crystals with GM, the density function is redefined with an additional property that takes into account the exposure time of the crystals to impurity. It is assumed that the transient coverage process can be described by a first order dynamics. The resulting PBMs are simulated using commercially available software gCRYSTAL (Process Systems Enterprise, UK) for 1D problems. On the other hand, well-established high resolution finite volume technique is used for simulation of all the 1D and multidimensional problems [7]. This study would be very useful in understanding the effect of GM as well as in achieving tailored crystal shape distribution.
References
[1] C. Borchert, N. Nere, D. Ramkrishna, A. Voigt and K. Sundmacher. On the prediction of crystal shape distributions in a steady-state continuous crystallizer. Chem. Eng. Sci., 64(4): 686-696, 2009.
[2] G. Yang, N. Kubota, Z. Sha, M. Louhi-Kultanen and J. Wang. Crystal shape control by manipulating supersaturation in batch cooling crystallization. Cryst. Growth Des., 6(12):2799-2803, 2006.
[3] C. Y. Ma and X. Z. Wang. Model identification of crystal facet growth kinetics in morphological population balance modeling of l-glutamic acid crystallization and experimental validation. Chem. Eng. Sci., 70(0):22-30, 2012.
[4] F. Fevotte and G. Fevotte. A method of characteristics for solving population balance equations (PBE) describing the adsorption of impurities during crystallization processes. Chem. Eng. Sci., 65(10):3191-3198, 2010.
[5] N. Kubota. Effect of impurities on growth kinetics. Cryst. Res. Technol., 36(8-10):749-769, 2001.
[6] N. Kubota and J. W. Mullin. A kinetic model for crystal growth from aqueous solution in the presence of impurity. J. Crys. Grow., 152(3):203-208, 1995.
[7] R. Gunawn, I. Fusman and R. D. Braatz. High resolution algorithm for multidimensional population balance equations. AIChE J, 50:2738-2749, 2006.