Flow visualization through spacer filled channels by computational fluid dynamics I. Pressure drop and shear rate calculations for flat sheet geometry

Citation
Sk. Karode et A. Kumar, Flow visualization through spacer filled channels by computational fluid dynamics I. Pressure drop and shear rate calculations for flat sheet geometry, J MEMBR SCI, 193(1), 2001, pp. 69-84
Citations number
11
Categorie Soggetti
Chemistry,"Chemical Engineering
Journal title
JOURNAL OF MEMBRANE SCIENCE
ISSN journal
03767388 → ACNP
Volume
193
Issue
1
Year of publication
2001
Pages
69 - 84
Database
ISI
SICI code
0376-7388(20011031)193:1<69:FVTSFC>2.0.ZU;2-6
Abstract
Computational fluid dynamics (CFD) simulations were carried out for fluid f low through rectangular channels filled with several commercially available spacers for membrane modules. Simulation results were compared with litera ture experimental data. Excellent agreement was found between the experimen tally determined dependence of the total drag coefficient on the Reynolds n umber and the CFD simulations in this work. Analysis of the flow structure through spacer filled channels revealed that bulk of the fluid does not cha nge direction at each mesh as suggested previously in the literature, but t hat the bulk fluid flows parallel to the spacer filaments. The pressure dro p through the channel was found to be largely governed by a loss of fluid m omentum caused due to an almost abrupt change in the direction of the veloc ity vectors across a thin transition plane corresponding to the plane of in tersection of the spacer filaments. It was observed that spacers with equal filament diameters usually result in a higher pressure drop across the cha nnel and such symmetric spacers also result in a more uniform shear rate at the top and bottom faces of the test cell. Asymmetric spacers (spacers wit h unequal filament diameters) resulted in lower pressure drop and also indu ced unequal shear rate on the top and bottom faces of the test cell. Such u nequal shear rates at the top and bottom faces would be expected to have an adverse impact on the membrane module performance because of different mas s transfer characteristics for adjacent membrane leaves. It was found that a higher overall bulk turbulent flow would not necessarily result in higher shear rates at the top and bottom faces. (C) 2001 Published by Elsevier Sc ience B.V.