Influence of substrate on fouling in anoxic immersed membrane bioreactors

被引:29
作者
McAdam, Ewan J. [1 ]
Judd, Simon J. [1 ]
Cartmell, Elise [1 ]
Jefferson, Bruce [1 ]
机构
[1] Cranfield Univ, Ctr Water Sci, Cranfield MK43 0AL, Beds, England
关键词
fouling; anoxic; membrane bioreactor; carbon substrate;
D O I
10.1016/j.watres.2007.05.017
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The influence of carbon substrate chemistry on membrane bioreactor (MBR) fouling in anoxic conditions has been evaluated. The use of a weak carboxylic acid (acetic acid) resulted in the production of large open-floc structures (up to 508 mu m) that were susceptible to breakage. Primary particles (d(10) and d(20) particle sizes, 5.5 +/- 1.3 and 15.3 +/- 8.2 mu m, respectively) and macromolecular soluble microbial products (SMPs) were generated, directly impacting on membrane fouling. The use of a primary alcohol (ethanol), on the other hand, encouraged the growth of flocs similar to activated sludge. These flocs produced low concentrations of primary particles (d(10) and d(20) particle sizes, 120.6 +/- 36.1 and 185.2 +/- 62.7 mu m, respectively) and high-molecular-weight SMP, and the particles had sufficient mechanical integrity to withstand shear. Consequently, the use of ethanol resulted in sufficient suppression of fouling to extend the filtration time by a factor of three. An increase in MLSS concentration did not directly impact upon fouling when operating with ethanol, primarily because of the low concentration of particulate matter produced. (c) 2007 Elsevier Ltd. All rights reserved.
引用
收藏
页码:3859 / 3867
页数:9
相关论文
共 29 条
[1]  
[Anonymous], STAND METH EX WAT WA
[2]   SOLUBLE MICROBIAL PRODUCT FORMATION IN BIOLOGICAL-SYSTEMS [J].
BOERO, VJ ;
ECKENFELDER, WW ;
BOWERS, AR .
WATER SCIENCE AND TECHNOLOGY, 1991, 23 (4-6) :1067-1076
[3]   Molecular weight distribution of soluble microbial products in biological systems [J].
Boero, VJ ;
Bowers, AR ;
Eckenfelder, WW .
WATER SCIENCE AND TECHNOLOGY, 1996, 34 (5-6) :241-248
[4]   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
[5]   DENITRIFICATION UNIT BIOCENOSIS [J].
GRABINSKALONIEWSKA, A .
WATER RESEARCH, 1991, 25 (12) :1565-1573
[6]   Characterization of DOM as a function of MW by fluorescence EEM and HPLC-SEC using UVA, DOC, and fluorescence detection [J].
Her, N ;
Amy, G ;
McKnight, D ;
Sohn, J ;
Yoon, YM .
WATER RESEARCH, 2003, 37 (17) :4295-4303
[7]   CONSTANT FLOW-RATE BLOCKING LAWS AND AN EXAMPLE OF THEIR APPLICATION TO DEAD-END MICROFILTRATION OF PROTEIN SOLUTIONS [J].
HLAVACEK, M ;
BOUCHET, F .
JOURNAL OF MEMBRANE SCIENCE, 1993, 82 (03) :285-295
[8]   Overview of fouling phenomena and modeling approaches for membrane bioreactors [J].
Ho, Chia-Chi ;
Zydney, Andrew L. .
SEPARATION SCIENCE AND TECHNOLOGY, 2006, 41 (07) :1231-1251
[9]   Chelating properties and molecular weight distribution of soluble microbial products from an aerobic membrane bioreactor [J].
Holakoo, Ladan ;
Nakhla, George ;
Yanful, Ernest K. ;
Bassi, Amarjeet S. .
WATER RESEARCH, 2006, 40 (08) :1531-1538
[10]   Comparison of membrane biofouling in nitrification and denitrification for the membrane bioreactor (MBR) [J].
Jang, N. ;
Ren, X. ;
Choi, K. ;
Kim, I. S. .
WATER SCIENCE AND TECHNOLOGY, 2006, 53 (06) :43-49