Effects of membrane fouling on solute rejection during membrane filtration of activated sludge

被引:164
作者
Chang, IS [1 ]
Bag, SO
Lee, CH
机构
[1] Hoseo Univ, Dept Environm Engn, Chung Nam 336795, South Korea
[2] Seoul Natl Univ, Sch Chem Engn, Seoul 151742, South Korea
关键词
activated sludge; fouling; membrane bioreactor (MBR); membrane; ultrafiltration;
D O I
10.1016/S0032-9592(00)00284-3
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
To assess the relationship between solute rejection and membrane fouling in a MBR system, membrane filtrations of activated sludge in different physiological states were carried out with ultrafiltration membranes. Regardless of the physiological states of the activated sludge (foaming, bulking, pin-point hoc, exponential growth. endogenous phase, normal state sludge), the hydrophobic membrane (PM30) always showed greater solute rejection than the hydrophilic membrane (YM30). To investigate the key factors affecting solute rejection, the cake layer resistances (R-c) and the fouling resistances (R-f) were measured. The R-c and R-f values for the PM30 were always higher than for the YM30 and the R-c prevailed over the R-f in all cases. The solutes rejection by the adsorption onto/into the membrane was relatively small. This suggests that the cake layer deposited on the membrane surfaces played an important role in the solute rejection, i.e. dominant solute removals were attributed to the adsorption and/or sieving onto the cakes. Consequently, the difference in solute rejection efficiency between hydrophilic and hydrophobic membranes was mainly due to the degree of sieving and/or adsorption onto the cakes deposited on the membrane, and partly due to adsorption into membrane pores and the surfaces. (C) 2001 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:855 / 860
页数:6
相关论文
共 16 条
[1]  
APHA AWWA WEF, 1995, STAND METH EX WAT WA
[2]   FACTORS AFFECTING FLUX IN CROSS-FLOW FILTRATION [J].
BAKER, RJ ;
FANE, AG ;
FELL, CJD ;
YOO, BH .
DESALINATION, 1985, 53 (1-3) :81-93
[3]   Membrane filtration characteristics in membrane-coupled activated sludge system: The effect of floc structure on membrane fouling [J].
Chang, IS ;
Lee, CH ;
Ahn, KH .
SEPARATION SCIENCE AND TECHNOLOGY, 1999, 34 (09) :1743-1758
[4]   Membrane filtration characteristics in membrane-coupled activated sludge system - the effect of physiological states of activated sludge on membrane fouling [J].
Chang, IS ;
Lee, CH .
DESALINATION, 1998, 120 (03) :221-233
[5]   Contribution of various constituents of activated sludge to membrane bioreactor fouling [J].
Defrance, L ;
Jaffrin, MY ;
Gupta, B ;
Paullier, P ;
Geaugey, V .
BIORESOURCE TECHNOLOGY, 2000, 73 (02) :105-112
[6]   Cross-flow filtration of an anaerobic methanogenic suspension [J].
Elmaleh, S ;
Abdelmoumni, L .
JOURNAL OF MEMBRANE SCIENCE, 1997, 131 (1-2) :261-274
[7]   ORGANIC WASTE-WATER TREATMENT BY ACTIVATED-SLUDGE PROCESS USING INTEGRATED TYPE MEMBRANE SEPARATION [J].
FUTAMURA, O ;
KATOH, M ;
TAKEUCHI, K .
DESALINATION, 1994, 98 (1-3) :17-25
[8]   Membrane bioreactors and their role in wastewater reuse [J].
Jefferson, B ;
Laine, AL ;
Judd, SL ;
Stephenson, T .
WATER SCIENCE AND TECHNOLOGY, 2000, 41 (01) :197-204
[9]   Bacterial rejection in crossflow microfiltration of sewage [J].
Judd, SJ ;
Till, SW .
DESALINATION, 2000, 127 (03) :251-260
[10]   Comparison of ultrafiltration characteristics between activated sludge and BAC sludge [J].
Kim, JS ;
Lee, CH ;
Chun, HD .
WATER RESEARCH, 1998, 32 (11) :3443-3451