Simulation of the flow around spacer filaments between channel walls. 2. Mass-transfer enhancement

被引:123
作者
Schwinge, J
Wiley, DE [1 ]
Fletcher, DF
机构
[1] Univ New S Wales, Sch Chem Engn & Ind Chem, UNESCO, Ctr Membrane Sci & Technol, Sydney, NSW 2052, Australia
[2] Univ Sydney, Dept Chem Engn, Sydney, NSW 2006, Australia
关键词
D O I
10.1021/ie011015o
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A computational fluid dynamics (CFD) code was used to study the effects of Reynolds number, mesh length, and filament diameter on mass-transfer enhancement for three spacer configurations a cavity, a zigzag, and a submerged spacer. For the cavity and zigzag spacers, mass-transfer, enhancement first increases with a decrease in the mesh length, reaches a maximum, and then decreases with a further decrease in the mesh length, while pressure loss showed a continuous increase with a decrease in the mesh length. The submerged spacer shows a continuous increase of the mass-transfer enhancement and pressure loss with a decrease in the mesh length. For all spacer types, mass transfer increases with the filament diameter. However, at a smaller filament diameter, the overall spacer performance increases, as indicated by a high mass-transfer enhancement to pressure loss ratio. Overall, the CFD simulations reveal that the zigzag spacer is the most efficient spacer type for a spiral wound membrane module.
引用
收藏
页码:4879 / 4888
页数:10
相关论文
共 20 条
[1]   EXPERIMENTAL STUDY OF ELECTRODIALYSIS HYDRODYNAMICS [J].
BELFORT, G ;
GUTER, GA .
DESALINATION, 1972, 10 (03) :221-&
[2]  
*CFX INT AEA TECHN, 2001, CFX 4 3 US MAN
[3]   Mass transfer (absorption) coefficients - Prediction from data on great transfer and fluid friction [J].
Chilton, TH ;
Colburn, AP .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1934, 26 :1183-1187
[4]  
DaCosta A.R., 1993, PhD thesis,
[5]   HEAT AND MASS-TRANSFER COMPUTATIONS FOR LAMINAR-FLOW IN AN AXISYMMETRIC SUDDEN EXPANSION [J].
FLETCHER, DF ;
MASKELL, SJ ;
PATRICK, MA .
COMPUTERS & FLUIDS, 1985, 13 (02) :207-221
[6]   ON THE MECHANISM OF TRANSFER ENHANCEMENT BY EDDY PROMOTERS [J].
FOCKE, WW .
ELECTROCHIMICA ACTA, 1983, 28 (08) :1137-1146
[7]   EFFECT OF VISCOSITY ON CONCENTRATION POLARIZATION IN ULTRAFILTRATION [J].
GILL, WN ;
WILEY, DE ;
FELL, CJD ;
FANE, AG .
AICHE JOURNAL, 1988, 34 (09) :1563-1567
[8]  
KANG IS, 1982, INT J HEAT MASS TRAN, V25, P1167, DOI 10.1016/0017-9310(82)90211-3
[9]   EXPERIMENTAL-STUDY OF MASS-TRANSFER AROUND A TURBULENCE PROMOTER BY THE LIMITING CURRENT METHOD [J].
KIM, DH ;
KIM, IH ;
CHANG, HN .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1983, 26 (07) :1007-1016
[10]   ENHANCED MASS-TRANSFER IN ELECTROCHEMICAL CELLS USING TURBULENCE PROMOTERS [J].
LEITZ, FB ;
MARINCIC, L .
JOURNAL OF APPLIED ELECTROCHEMISTRY, 1977, 7 (06) :473-484