Numerical study of two-dimensional multi-layer spacer designs for minimum drag and maximum mass transfer

被引:50
作者
Fimbres-Weihs, G. A. [1 ]
Wiley, D. E. [1 ]
机构
[1] Univ New S Wales, Ctr Membrane Sci & Technol, UNESCO, Sch Chem Engn & Ind Chem, Sydney, NSW 2052, Australia
基金
澳大利亚研究理事会;
关键词
Computational fluid dynamics; Mass transfer; Novel spacer; Spacer design; Multi-layer spacer;
D O I
10.1016/j.memsci.2008.09.005
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Based on the insights gained from previous published works, a series of multi-layer spacer designs for use in spiral wound membrane modules are proposed and evaluated via computational fluid dynamics simulations. The filament diameter to channel height ratio of traditional cylindrical filaments is reduced from 0.6 to 0.4 and 0.3, and one or two layers of elliptical filaments with various attack angles are introduced in the middle region of the channel. The mass transport equations are solved in conjunction with the momentum and continuity equations for a solute with Schmidt number of 600, and the hydraulic Reynolds number is varied from 50 up to 800. Spacer performance is evaluated via a basic permeate processing cost analysis. The proposed designs did not lower processing costs when operating at hydraulic Reynolds numbers above 200, but showed potential for reducing costs in the steady laminar flow regime, at hydraulic Reynolds numbers equal to or less than 200. Implications for design improvements of spacer meshes, such as extra layers of spacer filaments to direct the bulk flow towards the membrane walls, and changes to the filament profiles to reduce form drag are discussed. (C) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:809 / 822
页数:14
相关论文
共 42 条
[1]  
Anderson JD., 1997, HIST AERODYNAMICS
[2]   Multi-layer spacer geometries with improved mass transport [J].
Balster, J. ;
Punt, I. ;
Stamatialis, D. F. ;
Wessling, A. .
JOURNAL OF MEMBRANE SCIENCE, 2006, 282 (1-2) :351-361
[3]   EXPERIMENTAL STUDY OF ELECTRODIALYSIS HYDRODYNAMICS [J].
BELFORT, G ;
GUTER, GA .
DESALINATION, 1972, 10 (03) :221-&
[4]  
Bird R.B., 2006, TRANSPORT PHENOMENA, Vsecond, DOI 10.1002/aic.690070245
[5]   GENERAL EXPRESSION FOR CORRELATION OF RATES OF TRANSFER AND OTHER PHENOMENA [J].
CHURCHILL, SW ;
USAGI, R .
AICHE JOURNAL, 1972, 18 (06) :1121-+
[6]   OPTIMAL CHANNEL SPACER DESIGN FOR ULTRAFILTRATION [J].
DACOSTA, AR ;
FANE, AG ;
FELL, CJD ;
FRANKEN, ACM .
JOURNAL OF MEMBRANE SCIENCE, 1991, 62 (03) :275-291
[7]   NET-TYPE SPACERS - EFFECT OF CONFIGURATION ON FLUID-FLOW PATH AND ULTRAFILTRATION FLUX [J].
DACOSTA, AR ;
FANE, AG .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1994, 33 (07) :1845-1851
[8]   THE INFLUENCE OF SEPARATORS ON HYDRODYNAMICS AND MASS-TRANSFER IN NARROW CELLS - FLOW VISUALIZATION [J].
FERON, P ;
SOLT, GS .
DESALINATION, 1991, 84 (1-3) :137-152
[9]   Numerical study of mass transfer in three-dimensional spacer-filled narrow channels with steady flow [J].
Fimbres-Weihs, G. A. ;
Wiley, D. E. .
JOURNAL OF MEMBRANE SCIENCE, 2007, 306 (1-2) :228-243
[10]   Unsteady flows with mass transfer in narrow zigzag spacer-filled channels: A numerical study [J].
Fimbres-Weihs, G. A. ;
Wiley, D. E. ;
Fletcher, D. F. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (19) :6594-6603