Influence of membrane properties on fouling in submerged membrane bioreactors

被引:125
作者
van der Marel, Perry [1 ,2 ]
Zwijnenburg, Arie [2 ]
Kemperman, Antoine [1 ]
Wessling, Matthias [1 ]
Temmink, Hardy [2 ,3 ]
van der Meer, Walter [1 ,2 ]
机构
[1] Univ Twente, Fac Sci & Technol, Membrane Technol Grp, IMPACT Inst Mech Proc & Control Twente, NL-7500 AE Enschede, Netherlands
[2] Ctr Excellence Sustainable Water Technol, NL-8900 CC Leeuwarden, Netherlands
[3] Wageningen Univ, Dept Environm Technol, NL-6700 EV Wageningen, Netherlands
关键词
Improved flux-step method; Critical flux and critical flux for irreversibility; Fouling reversibility; MBR; WASTE-WATER TREATMENT; CROSS-FLOW MICROFILTRATION; SUBCRITICAL FLUX OPERATION; ACTIVATED-SLUDGE; STEP METHOD; FILTRATION; ULTRAFILTRATION; DEPOSITION; MORPHOLOGY; COLLOIDS;
D O I
10.1016/j.memsci.2009.10.054
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Polymeric flat-sheet membranes with different properties were used in filtration experiments with activated sludge from a pilot-scale MBR to investigate the influence of membrane pore size, surface porosity, pore morphology, and hydrophobicity on membrane fouling. An improved flux-step method was used to measure both the critical flux and critical flux for irreversibility. Long term experiments were performed to evaluate if influences of membrane properties on short term could be translated to long term fouling behavior. The results showed that a hydrophilic asymmetric membrane with an interconnected pore structure, a nominal pore size of 0.3 mu m, and large surface porosity of 27%, provided the best membrane performance with respect to critical flux and critical flux for irreversibility. The dominant fouling mechanism in long term filtration experiments was gel layer formation, which for this membrane was the least severe, and therefore extended the sustainable time. (C) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:66 / 74
页数:9
相关论文
共 40 条
[1]  
ANDREOTTOLA G, 2003, P IMSTEC SYDN AUSTR
[2]   CAKE GROWTH-MECHANISM IN CROSS-FLOW MICROFILTRATION OF MINERAL SUSPENSIONS [J].
BENKAHLA, YK ;
OULDDRIS, A ;
JAFFRIN, MY ;
HASSEN, DS .
JOURNAL OF MEMBRANE SCIENCE, 1995, 98 (1-2) :107-117
[3]   Membrane fouling in membrane bioreactors for wastewater treatment [J].
Chang, IS ;
Le Clech, P ;
Jefferson, B ;
Judd, S .
JOURNAL OF ENVIRONMENTAL ENGINEERING, 2002, 128 (11) :1018-1029
[4]   Effects of membrane fouling on solute rejection during membrane filtration of activated sludge [J].
Chang, IS ;
Bag, SO ;
Lee, CH .
PROCESS BIOCHEMISTRY, 2001, 36 (8-9) :855-860
[5]   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
[6]   Particle deposition during membrane filtration of colloids: Transition between concentration polarization and cake formation [J].
Chen, V ;
Fane, AG ;
Madaeni, S ;
Wenten, IG .
JOURNAL OF MEMBRANE SCIENCE, 1997, 125 (01) :109-122
[7]   Performance of partially permeable microfiltration membranes under low fouling conditions [J].
Chen, V .
JOURNAL OF MEMBRANE SCIENCE, 1998, 147 (02) :265-278
[8]   Fouling transients in nominally sub-critical flux operation of a membrane bioreactor [J].
Cho, BD ;
Fane, AG .
JOURNAL OF MEMBRANE SCIENCE, 2002, 209 (02) :391-403
[9]  
CHOI JH, 2007, P IWA C HARR
[10]   Reversibility of fouling formed in activated sludge filtration [J].
Defrance, L ;
Jaffrin, MY .
JOURNAL OF MEMBRANE SCIENCE, 1999, 157 (01) :73-84