Air sparging in ultrafiltration hollow fibers:: relationship between flux enhancement, cake characteristics and hydrodynamic parameters

被引:130
作者
Cabassud, C
Laborie, S
Durand-Bourlier, L
Lainé, JM
机构
[1] Inst Natl Sci Appl, Dept Genie Proc Ind, Lab Ingn Proc Environm, F-31077 Toulouse 4, France
[2] Cirsee Lyonnaise Eaux, F-78230 Le Pecq, France
关键词
air sparging; hollow fibers; ultrafiltration; drinking water; flux enhancement; two-phase flow; wall shear stress; cake characteristics; future trends;
D O I
10.1016/S0376-7388(00)00538-X
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The gas sparging process consists in injecting a gas with the feed during the filtration period. Many studies have recently demonstrated the interest of gas sparging for various membrane configurations to enhance the flux or to modify the membrane selectivity. This study focuses on gas sparging in ultrafiltration hollow fibers to prevent a particulate deposit. New experimental results on ultrafiltration of river water are introduced and demonstrate that air sparging is more interesting for waters having a high fouling ability (low critical flux). On the basis of experimental results for clay suspensions, an analysis of the influence of the two-phase flow parameters on the cake characteristics (porosity, thickness and specific resistance) is then introduced and allows to demonstrate that the notion of cake deposit is no more available with a gas/liquid flow. Hydrodynamics of the gas/liquid two-phase how was characterized, in order to identify the parameters responsible for deposit prevention and for flux enhancement. Mixing or turbulence near the membrane surface seems to control the flux enhancement whereas the cake structure seems to be linked either to mixing or to the flow intermittence. To conclude, perspectives of future processes which could involve air sparging are discussed. (C) 2001 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:57 / 69
页数:13
相关论文
共 16 条
[1]   Gas sparging to enhance permeate flux in ultrafiltration using hollow fibre membranes [J].
Bellara, SR ;
Cui, ZF ;
Pepper, DS .
JOURNAL OF MEMBRANE SCIENCE, 1996, 121 (02) :175-184
[2]   How slug flow can improve ultrafiltration flux in organic hollow fibres [J].
Cabassud, C ;
Laborie, S ;
Laine, JM .
JOURNAL OF MEMBRANE SCIENCE, 1997, 128 (01) :93-101
[3]   Flux enhancements with gas sparging in downwards crossflow ultrafiltration: Performance and mechanism [J].
Cui, ZF ;
Wright, KIT .
JOURNAL OF MEMBRANE SCIENCE, 1996, 117 (1-2) :109-116
[4]   GAS-LIQUID 2-PHASE CROSS-FLOW ULTRAFILTRATION OF BSA AND DEXTRAN SOLUTIONS [J].
CUI, ZF ;
WRIGHT, KIT .
JOURNAL OF MEMBRANE SCIENCE, 1994, 90 (1-2) :183-189
[5]  
CUI ZF, EFFECTIVE MEMBRANE P, P237
[6]  
DUCOM G, 2000, CASE STABILISED EMUL, V1, P635
[7]  
Fabre J, 1996, INT ENCY HEAT MASS T, P1015
[8]   Flux enhancement by a continuous tangential gas flow in ultrafiltration hollow fibres for drinking water production: Effects of slug flow on cake structure [J].
Laborie, S ;
Cabassud, C ;
DurandBourlier, L ;
Laine, JM .
FILTRATION & SEPARATION, 1997, 34 (08) :887-891
[9]   Fouling control by air sparging inside hollow fibre membranes - effects on energy consumption [J].
Laborie, S ;
Cabassud, C ;
Durand-Bourlier, L ;
Laine, JM .
DESALINATION, 1998, 118 (1-3) :189-196
[10]   Characterisation of gas-liquid two-phase flow inside capillaries [J].
Laborie, S ;
Cabassud, C ;
Durand-Bourlier, L ;
Lainé, JM .
CHEMICAL ENGINEERING SCIENCE, 1999, 54 (23) :5723-5735