Process Systems Engineering
Predictions of porosity and fluid distribution through nonspherical-packed columns
Article first published online: 7 JUL 2011
DOI: 10.1002/aic.12691
Copyright © 2011 American Institute of Chemical Engineers (AIChE)
Additional Information
How to Cite
Caulkin, R., Jia, X., Fairweather, M. and Williams, R. A. (2012), Predictions of porosity and fluid distribution through nonspherical-packed columns. AIChE J., 58: 1503–1512. doi: 10.1002/aic.12691
Publication History
- Issue published online: 6 APR 2012
- Article first published online: 7 JUL 2011
- Accepted manuscript online: 24 MAY 2011 10:31AM EST
- Manuscript Revised: 20 MAY 2011
- Manuscript Received: 30 NOV 2009
- Abstract
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Keywords:
- chemical reactors;
- packed bed;
- simulation;
- voidage;
- fluid velocity distribution
Abstract
For beds comprised randomly arranged nonspherical particles, the prediction and understanding of the packing characteristics and subsequent fluid flow through the resulting porous media is a longstanding problem for chemical and process engineers. This paper presents the application of a digital modeling approach to particle packing, in which no more than elementary physical concepts are used, with the model using collision points to predict trends in bed structures of particles of different geometry. Lattice Boltzmann modeling (LBM), coupled to the output of the packing model, is used to subsequently assess velocity distribution through the generated structures. Simulation results are compared with data available from the literature, as a means of model validation, where it is demonstrated that the combined approach of the digital packing algorithm and LBM provide a modeling capability that is of value to a range of engineering applications. © 2011 American Institute of Chemical Engineers AIChE J, 2012

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