Characterization and modeling of the soluble microbial products in membrane bioreactor

被引:56
作者
Tian, Yu [1 ,2 ]
Chen, Lin [1 ]
Jiang, Tianling [1 ]
机构
[1] Harbin Inst Technol, Sch Municipal & Environm Engn, Harbin 150090, Peoples R China
[2] Harbin Inst Technol, State Key Lab Urban Water Resource & Environm, Harbin 150090, Peoples R China
关键词
Membrane bioreactor; Modeling; Soluble microbial products; Utilization-associated products; Biomass-associated products; WASTE-WATER TREATMENT; EXTRACELLULAR POLYMERIC SUBSTANCES; DISSOLVED ORGANIC-MATTER; ACTIVATED-SLUDGE; SIMULTANEOUS STORAGE; AEROBIC CONDITIONS; GROWTH-PROCESSES; MBR; DEGRADATION; EXCITATION;
D O I
10.1016/j.seppur.2010.10.022
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The presence of soluble microbial products (SMP), including utilization-associated products (UAP) and biomass-associated products (BAP), is of great importance to membrane fouling problem. In this study, characterization and modeling of the SMP were conducted towards a better understanding of the production and composition of SMP in the membrane bioreactor (MBR). Based on the chemical analysis, both UAP and BAP exhibited the biodegradability and had a large fraction of molecular weight greater than 20 kDa, thus hydrolysis was assumed as the first step for SMP utilization. The simulation of biological processes was described on the platform of activated sludge model 3 (ASM3) with two main modifications: (i) adopting the concept of simultaneous growth and storage of organic substrates by heterotrophic bacteria; (ii) introducing the formation and degradation of SMP into the biological processes. Batch experimental results were used for SMP parameter estimations, and simulation results showed that the model was able to describe the SMP dynamics and provide further insights into MBR operations. The effect of the sludge retention time (SRT) and hydraulic retention time (HRT) on the formation of SMP could therefore be analyzed by model simulation: a minimum SMP production with 25.1 mg COD/L was suggested at 40 days SRT and 8 h HRT. (c) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:316 / 324
页数:9
相关论文
共 33 条
[1]  
[Anonymous], 1995, Standard methods for examination of water and waste water, V19th
[2]   Impact of molecular weight distribution of soluble microbial products on fouling in membrane bioreactors [J].
Arabi, Sara ;
Nakhla, George .
SEPARATION AND PURIFICATION TECHNOLOGY, 2010, 73 (03) :391-396
[3]   A review of soluble microbial products (SMP) in wastewater treatment systems [J].
Barker, DJ ;
Stuckey, DC .
WATER RESEARCH, 1999, 33 (14) :3063-3082
[4]   Fouling characterisation in membrane bioreactors [J].
Bouhabila, E ;
Ben Aïm, R ;
Buisson, H .
SEPARATION AND PURIFICATION TECHNOLOGY, 2001, 22-3 (1-3) :123-132
[5]   Fluorescence excitation - Emission matrix regional integration to quantify spectra for dissolved organic matter [J].
Chen, W ;
Westerhoff, P ;
Leenheer, JA ;
Booksh, K .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 2003, 37 (24) :5701-5710
[6]   An integrated model for physical-biological wastewater organic removal in a submerged membrane bioreactor: Model development and parameter estimation [J].
Di Bella, Gaetano ;
Mannina, Giorgio ;
Viviani, Gaspare .
JOURNAL OF MEMBRANE SCIENCE, 2008, 322 (01) :1-12
[7]  
Dochain D., 2001, Dynamic modelling and estimation in wastewater treatment processes
[8]   A COLORIMETRIC METHOD FOR THE DETERMINATION OF SUGARS [J].
DUBOIS, M ;
GILLES, K ;
HAMILTON, JK ;
REBERS, PA ;
SMITH, F .
NATURE, 1951, 168 (4265) :167-167
[9]   Activated sludge model (ASM) based modelling of membrane bioreactor (MBR) processes: A critical review with special regard to MBR specificities [J].
Fenu, A. ;
Guglielmi, G. ;
Jimenez, J. ;
Sperandio, M. ;
Saroj, D. ;
Lesjean, B. ;
Brepols, C. ;
Thoeye, C. ;
Nopens, I. .
WATER RESEARCH, 2010, 44 (15) :4272-4294
[10]  
Henze M., 2006, Activated Sludge Models ASM1, ASM2, ASM2d and ASM3