Multi-Scale Modeling of Industrial Crystallization Process

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Abstract:

The multi-scale method was applied to solve the multi-phase multi-scale problem in the industrial crystallization process. The fluid dynamics model was considering under the grid scale, and the population balance model was considering under subsystem scale. The macro model was used to interact with the environment. The crystallization process of potassium chloride was simulated by CFD and MATLAB. The result of the simulation shows the distribution of the supersaturation is strongly affected by the distribution of the suspended crystal volume fraction.

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3062-3066

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February 2013

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© 2013 Trans Tech Publications Ltd. All Rights Reserved

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[1] Li. J., Kwauk M., Ind. Eng. Chem. Res., 40 (2001), 4227-4237.

Google Scholar

[2] Gates T. S., Odegard G. M., Frankland S. J. V., Clancy T. C., Composites Science and Technology, 65 (2005), 2416-2434.

DOI: 10.1016/j.compscitech.2005.06.009

Google Scholar

[3] Kramer H. J. M., Beringham S. K., van Rosmalen G. M., Journal of crystal growth, 199 (1999), 729-737.

Google Scholar

[4] Ma A. L., Tafti A. K., Braatz R. D., Computers and Chemical Engineering, 26 (2002), 1103-1116.

Google Scholar

[5] Kulikov V., Briesen H. and Marquardt W., Chemical Engineering Research and design, 83 (2005), 706-717.

Google Scholar

[6] Sha Z. Palossari S., Chemical Engineering Science, 55 (2000), 1797-1806.

Google Scholar

[7] J.H. Ferziger, M. Peri ´c, Computational Methods for Fluid Dynamics (Springer-Verlag, Berlin 1997).

Google Scholar

[8] Qian R Y, Fang X S, Wang Z K, Ind. Eng. Chem. Res., 28 (1989), 844-85.

Google Scholar