The effect of mixed liquor suspended solids (MLSS) on biofouling in a hybrid membrane bioreactor for the treatment of high concentration organic wastewater

被引:29
作者
Damayanti, A. [1 ]
Ujang, Z. [1 ]
Salim, M. R. [1 ]
Olsson, G. [2 ]
机构
[1] Univ Teknol Malaysia UTM, Inst Environm & Water Resource Management IPASA, Skudai 81310, Johor Bahru, Malaysia
[2] Lund Univ, Ind Elect Engn & Automat IEA, SE-22100 Lund, Sweden
关键词
biofouling; flux; membrane bioreactor; MLSS; TMP; OIL MILL EFFLUENT; ACTIVATED-SLUDGE; CRITICAL FLUX; FILTRATION; GROWTH; PLANT;
D O I
10.2166/wst.2011.338
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Biofouling is a crucial factor in membrane bioreactor (MBR) applications, particularly for high organic loading operations. This paper reports a study on biofouling in an MBR to establish a relationship between critical flux, J(c), mixed liquor suspended solids (MLSS) (ranging from 5 to 20 g L-1) and volumetric loading rate (6.3 kg COD m(-3) h(-1)) of palm oil mill effluent (POME). A lab-scale 100 L hybrid MBR consisting of anaerobic, anoxic, and aerobic reactors was used with flat sheet microfiltration (MF) submerged in the aerobic compartment. The food-to-microorganism (F/M) ratio was maintained at 0.18 kg COD kg(-1) MLSSd(-1). The biofouling tendency of the membrane was obtained based on the flux against the transmembrane pressure (TMP) behaviour. The critical flux is sensitive to the MLSS. At the MLSS 20 g L-1 the critical flux is about four times lower than that for the MLSS concentration of 5 g L-1. The results showed high removal efficiency of denitrification and nitrification up to 97% at the MLSS concentration 20 g L-1. The results show that the operation has to compromise between a high and a low MLSS concentration. The former will favour a higher removal rate, while the latter will favour a higher critical flux.
引用
收藏
页码:1701 / 1706
页数:6
相关论文
共 22 条
[1]  
Ahmad Z., 2008, AS WAT C KUAL LUMP
[2]  
Alaboud T. M., 2009, Research Journal of Environmental Sciences, V3, P267, DOI 10.3923/rjes.2009.267.277
[3]   Settling behaviour of aerobic granular sludge [J].
Anuar, A. Nor ;
Ujang, Z. ;
van Loosdrecht, M. C. M. ;
de Kreuk, M. K. .
WATER SCIENCE AND TECHNOLOGY, 2007, 56 (07) :55-63
[4]  
APHA (AMERICAN PUBLIC HEALTH ASSOCIATION), 1995, Standard Methods for the Examination of Water and Waste Water
[5]   Critical flux in submerged membrane bioreactors for municipal wastewater treatment [J].
Bottino, A. ;
Capannelli, G. ;
Comite, A. ;
Mangano, R. .
DESALINATION, 2009, 245 (1-3) :748-753
[6]   Wastewater treatment using membrane filtration - effect of biosolids concentration on cake resistance [J].
Chang, IS ;
Kim, SN .
PROCESS BIOCHEMISTRY, 2005, 40 (3-4) :1307-1314
[7]   Respirometric analysis of activated sludge models from palm oil mill effluent [J].
Damayanti, A. ;
Ujang, Z. ;
Salim, M. R. ;
Olsson, G. ;
Sulaiman, A. Z. .
BIORESOURCE TECHNOLOGY, 2010, 101 (01) :144-149
[8]  
Hamdzah M., 2005, REVERSE OSMOSIS RO M
[9]   Effect of temperature and pH on growth and product formation of Lactococcus lactis ssp lactis ATCC 19435 growing on maltose [J].
Hofvendahl, K ;
van Niel, EWJ ;
Hahn-Hägerdal, B .
APPLIED MICROBIOLOGY AND BIOTECHNOLOGY, 1999, 51 (05) :669-672
[10]   Separation and concentration of cobalt from zinc plant acidic thiocyanate leach solutions containing cobalt and nickel by an emulsion liquid membrane using triisooctylamine as carrier [J].
Kumbasar, Recep Ali .
JOURNAL OF MEMBRANE SCIENCE, 2009, 333 (1-2) :118-124