Internal versus external submerged membrane bioreactor configurations for dairy wastewater treatment

被引:17
作者
de Andrade, Laura Hamdan [1 ]
dos Santos Mendes, Flavia Daniele [1 ]
Espindola, Jonathan Cawettiere [1 ]
Santos Amaral, Miriam Cristina [1 ]
机构
[1] Univ Fed Minas Gerais, Dept Sanit & Environm Engn, Belo Horizonte, MG, Brazil
关键词
Soluble microbial products (SMP); Fouling; Dairy wastewater; Submerged membrane bioreactor (SMBR) configuration; Extracellular polymeric substances (EPS); EXTRACELLULAR POLYMERIC SUBSTANCES; EXOPOLYMER PARTICLES TEP; ACTIVATED-SLUDGE; CHEESE WHEY; WASTEWATERS; PERFORMANCE; FILTRATION; MBRS;
D O I
10.1080/19443994.2013.799048
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Two submerged membrane bioreactor (SMBR) configurations, one with the membrane module internal (SMBRi) and the other one external (SMBRe) to the biological tank, were used for the treatment of dairy industry effluent and evaluated in terms of pollutant removal capacity and fouling, focusing on the production of soluble microbial products (SMP) and extracellular polymeric substances (EPS). Both the MBRs presented excellent chemical oxygen demand (COD) removal efficiency (98% average), color (98%), and nutrients (86% for total nitrogen and 86-89% for total phosphorus); however, it was shown that shearing caused by the sludge recirculation pumps in the SMBRe reduced biomass growth considerably. The SMBRe presented better performance in terms of fouling than the SMBRi, which was associated with the higher concentration of suspended solids and SMP and EPS in the SMBRi. The SMP concentrations (mgSMP/gMLVSS) were superior in the SMBRe, showing that the friction from recirculation pumps leads to the breakdown of flocs and/or cells and to the release of polymeric material into the mixed liquor. Since this effect was more intense for SMP quantified in terms of extracellular transparent polymers, the conclusion was that apparently these substances participate in cellular metabolism in a different way than the carbohydrates and proteins, and that these can be more associated with released substances due to shear stress.
引用
收藏
页码:2920 / 2932
页数:13
相关论文
共 43 条
[1]  
Amaral M.C.S., 2009, THESIS FEDERAL U MIN
[2]  
Andrade L.H., 2011, THESIS FEDERAL U MIN
[3]  
[Anonymous], 2005, Standard methods for the examination of water and waste- water
[4]   Treatment of two industrial wastewaters in a submerged membrane bioreactor [J].
Artiga, P ;
Ficara, E ;
Malpei, F ;
Garrido, JM ;
Méndez, R .
DESALINATION, 2005, 179 (1-3) :161-169
[5]   Immersed Membrane BioReactor (IMBR) for treatment of combined domestic and dairy wastewater in an isolated farm: An exploratory case study implementing the Facet Analysis (FA) [J].
Bick, Amos ;
Plazas T, Jaime G. ;
Yang, Fei ;
Raveh, Adi ;
Hagin, Josef ;
Oron, Gideon .
DESALINATION, 2009, 249 (03) :1217-1222
[6]   Fouling characterisation in membrane bioreactors [J].
Bouhabila, E ;
Ben Aïm, R ;
Buisson, H .
SEPARATION AND PURIFICATION TECHNOLOGY, 2001, 22-3 (1-3) :123-132
[7]   Computational fluid dynamics simulations of MBRs: Inside submerged versus outside submerged membranes [J].
Brannock, M. W. D. ;
De Wever, Heleen ;
Wang, Y. ;
Leslie, G. .
DESALINATION, 2009, 236 (1-3) :244-251
[8]   MBR module design and operation [J].
Buer, Thomas ;
Cumin, Jeff .
DESALINATION, 2010, 250 (03) :1073-1077
[9]  
Bura R, 1998, WATER SCI TECHNOL, V37, P325, DOI 10.2166/wst.1998.0657
[10]   A review on hydrolytic enzymes in the treatment of wastewater with high oil and grease content [J].
Cammarota, M. C. ;
Freire, D. M. G. .
BIORESOURCE TECHNOLOGY, 2006, 97 (17) :2195-2210