RO membrane solute rejection behavior at the initial stage of colloidal fouling

被引:12
作者
Ng, HY [1 ]
机构
[1] Natl Univ Singapore, Dept Civil Engn, Ctr Water Res, Singapore 117576, Singapore
关键词
reverse osmosis; colloidal fouling; flux decline; salt rejection; organic rejection; cake-enhanced concentration polarization;
D O I
10.1016/j.desal.2004.09.011
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This study investigated the rejection of salt and inert organic compounds by reverse osmosis membranes during the initial stage of colloidal fouling. Results of laboratory-scale experiments showed that colloidal fouling caused a marked decrease in flux, salt rejection and rejection of organics with molecular weight (MW) smaller than about 100 g/mol. Removal of neutrally charged organics was mainly by size or steric exclusion. Rejection of xylose, which has MW > 100 g/mol, was not affected much by colloidal fouling. The decrease in salt and low MW organic rejections during the initial stage of colloidal fouling was attributed to cake-enhanced concentration polarization, whereby the colloidal cake layer hindered back diffusion of solutes from the membrane surface to the bulk solution, resulting in higher solute concentration gradient across the membrane. At higher channel wall shear rate, the rates of colloidal deposition, flux decline, decrease in salt rejection, and decrease in low MW organic rejection were lower.
引用
收藏
页码:211 / 217
页数:7
相关论文
共 22 条
[1]   ARTIFICIAL PARTICULATE FOULING OF HYPERFILTRATION MEMBRANES [J].
BELFORT, G ;
ALEXANDROWICZ, G ;
MARX, B .
DESALINATION, 1976, 19 (1-3) :127-138
[2]   COLLOIDAL FOULING OF REVERSE-OSMOSIS MEMBRANES [J].
COHEN, RD ;
PROBSTEIN, RF .
JOURNAL OF COLLOID AND INTERFACE SCIENCE, 1986, 114 (01) :194-207
[3]   MODELING OF FOULING OF CROSS-FLOW MICROFILTRATION MEMBRANES [J].
DAVIS, RH .
SEPARATION AND PURIFICATION METHODS, 1992, 21 (02) :75-126
[4]  
DUVEL WA, 1975, J WATER POLLUT CON F, V47, P57
[5]   Effect of interparticle electrostatic double layer interactions on permeate flux decline in crossflow membrane filtration of colloidal suspensions: An experimental investigation [J].
Faibish, RS ;
Elimelech, M ;
Cohen, Y .
JOURNAL OF COLLOID AND INTERFACE SCIENCE, 1998, 204 (01) :77-86
[6]   REVERSE-OSMOSIS SEPARATION OF POLAR ORGANIC COMPOUNDS IN AQUEOUS-SOLUTION [J].
FANG, HHP ;
CHIAN, ESK .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 1976, 10 (04) :364-369
[7]   CALCIUM-SULFATE FOULING OF REVERSE-OSMOSIS MEMBRANES - FLUX DECLINE MECHANISM [J].
GILRON, J ;
HASSON, D .
CHEMICAL ENGINEERING SCIENCE, 1987, 42 (10) :2351-2360
[8]   Influence of crossflow membrane filter geometry and shear rate on colloidal fouling in reverse osmosis and nanofiltration separations [J].
Hoek, EMV ;
Kim, AS ;
Elimelech, M .
ENVIRONMENTAL ENGINEERING SCIENCE, 2002, 19 (06) :357-372
[9]   FT30 membranes of characterized porosities in the reverse osmosis organics removal from aqueous solutions [J].
KastelanKunst, L ;
Kosutic, K ;
Dananic, V ;
Kunst, B .
WATER RESEARCH, 1997, 31 (11) :2878-2884
[10]   THE EFFECTS OF MOLECULAR WIDTH ON PERMEATION OF ORGANIC SOLUTE THROUGH CELLULOSE-ACETATE REVERSE-OSMOSIS MEMBRANES [J].
KISO, Y ;
KITAO, T ;
JINNO, K ;
MIYAGI, M .
JOURNAL OF MEMBRANE SCIENCE, 1992, 74 (1-2) :95-103