Investigations into the effects of mass transport and flow dynamics of spacer filled membrane modules using CFD

被引:56
|
作者
Saeed, Asim [1 ]
Vuthaluru, Rupa [2 ]
Vuthaluru, Hari B. [2 ]
机构
[1] ACEPT, Challenger Inst Technol, Perth, WA 6166, Australia
[2] Curtin Univ, Sch Chem & Petr Engn, Perth, WA 6845, Australia
来源
关键词
Membranes; Reverse osmosis; Mass transport; Fouling; Fluid dynamics; SPIRAL-WOUND MODULES; OF-THE-ART; FLUID-DYNAMICS; PRESSURE-DROP; CONCENTRATION POLARIZATION; TURBULENCE PROMOTERS; CHANNELS; FLAT; GEOMETRY; VISUALIZATION;
D O I
10.1016/j.cherd.2014.07.002
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Cross-flow membrane operations often experience material build-up on membrane surfaces leading to maintenance issues. Although several studies addressed the flow distributions and concentration patterns during membrane operations, the prediction of fouling propensities of top and bottom membranes are non-existent. Present study investigates the effects of dimensionless filament spacing of feed spacer on flow and concentration patterns on membrane surfaces. Comparisons of spacers in terms of a novel concept 'Spacer Configuration Efficacy', SCE (Sh/Pn) revealed that spacers with higher SCE values would lead to higher mass transport of the solute away from the membrane walls with moderate energy losses. Among the 16 spacer arrangements studied, spacer with filament spacing of 4 was found to be the optimal (Re-h up to 200) with moderate pressure drop and higher values of mass transfer coefficient for the two membrane walls, further mass transfer coefficient values for the two membrane surfaces were found to be equal which leads to equal and lower fouling tendencies of the membrane walls. (C) 2014 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:79 / 99
页数:21
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