Flow of power law liquids through particle assemblages at intermediate Reynolds numbers

Jaiswal, A. K. ; Sundararajan, T. ; Chhabra, R. P. (1991) Flow of power law liquids through particle assemblages at intermediate Reynolds numbers The Canadian Journal of Chemical Engineering, 69 (6). pp. 1235-1241. ISSN 0008-4034

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Official URL: http://onlinelibrary.wiley.com/doi/10.1002/cjce.54...

Related URL: http://dx.doi.org/10.1002/cjce.5450690602

Abstract

The complete equations of motion and continuity have been solved numerically using the finite element method for the flow of power law liquids through assemblages of rigid spherical particles. The inter-particle interactions have been simulated using the free surface cell model. Extensive results on drag coefficients have been obtained under a wide range of physical and operating conditions (0.9999 ≥ 0.3), 1 ≥ n ≥ 0.4 and 20 ≥ Re ≥ 1. The observed dependence of drag coefficient on voidage and non-Newtonian flow behaviour index have been explained qualitatively with the aid of order of magnitude considerations. Finally, the theoretical predictions have been validated using suitable experimental data available in the literature.

Item Type:Article
Source:Copyright of this article belongs to John Wiley and Sons.
Keywords:Cell Model; Non-Newtonian Flow; Packed Beds; Power Law Liquid; Drag Coefficient
ID Code:78648
Deposited On:20 Jan 2012 11:57
Last Modified:20 Jan 2012 11:57

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