BSM-MBR: A benchmark simulation model to compare control and operational strategies for membrane bioreactors

被引:69
作者
Maere, Thomas [1 ]
Verrecht, Bart [2 ]
Moerenhout, Stefanie [1 ]
Judd, Simon [2 ]
Nopens, Ingmar [1 ]
机构
[1] Univ Ghent, BIOMATH, Dept Appl Math Biometr & Proc Control, B-9000 Ghent, Belgium
[2] Cranfield Univ, SIMS, Sch Water Sci, Cranfield MK43 0AL, Beds, England
关键词
BSM; Control; MBR; Modelling; Operational cost; Optimization; PERFORMANCE EVALUATION; OXYGEN-TRANSFER; DESIGN; COST; AERATION; EUROPE; STATE; WATER;
D O I
10.1016/j.watres.2011.01.006
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A benchmark simulation model for membrane bioreactors (BSM-MBR) was developed to evaluate operational and control strategies in terms of effluent quality and operational costs. The configuration of the existing BSM1 for conventional wastewater treatment plants was adapted using reactor volumes, pumped sludge flows and membrane filtration for the water-sludge separation. The BSM1 performance criteria were extended for an MBR taking into account additional pumping requirements for permeate production and aeration requirements for membrane fouling prevention. To incorporate the effects of elevated sludge concentrations on aeration efficiency and costs a dedicated aeration model was adopted. Steady-state and dynamic simulations revealed BSM-MBR, as expected, to outperform BSM1 for effluent quality, mainly due to complete retention of solids and improved ammonium removal from extensive aeration combined with higher biomass levels. However, this was at the expense of significantly higher operational costs. A comparison with three large-scale MBRs showed BSM-MBR energy costs to be realistic. The membrane aeration costs for the open loop simulations were rather high, attributed to non-optimization of BSM-MBR. As proof of concept two closed loop simulations were run to demonstrate the usefulness of BSM-MBR for identifying control strategies to lower operational costs without compromising effluent quality. (C) 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:2181 / 2190
页数:10
相关论文
共 31 条
[1]  
Alex J., 2008, BENCHMARK SIMULATION
[2]   THE CONCENTRATION AND ISOTOPIC FRACTIONATION OF OXYGEN DISSOLVED IN FRESH-WATER AND SEAWATER IN EQUILIBRIUM WITH THE ATMOSPHERE [J].
BENSON, BB ;
KRAUSE, D .
LIMNOLOGY AND OCEANOGRAPHY, 1984, 29 (03) :620-632
[3]   Considerations on the design and financial feasibility of full-scale membrane bioreactors for municipal applications [J].
Brepols, Ch. ;
Schaefer, H. ;
Engelhardt, N. .
WATER SCIENCE AND TECHNOLOGY, 2010, 61 (10) :2461-2468
[4]  
Copp J.B., 2002, The COST simulation benchmark-Description and simulator manual
[5]  
DEWEVER H, 2009, FIN MBR NETW WORKSH
[6]   Energy audit of a full scale MBR system [J].
Fenu, A. ;
Roels, J. ;
Wambecq, T. ;
De Gussem, K. ;
Thoeye, C. ;
De Gueldre, G. ;
Van De Steene, B. .
DESALINATION, 2010, 262 (1-3) :121-128
[7]   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
[8]  
GARCES A, 2007, 4 IWA INT MEMBR C ME
[9]   Biomass effects on oxygen transfer in membrane bioreactors [J].
Germain, E. ;
Nelles, F. ;
Drews, A. ;
Pearce, R. ;
Kraume, M. ;
Reid, E. ;
Judd, S. J. ;
Stephenson, T. .
WATER RESEARCH, 2007, 41 (05) :1038-1044
[10]   Activated sludge wastewater treatment plant modelling and simulation: state of the art [J].
Gernaey, KV ;
van Loosdrecht, MCM ;
Henze, M ;
Lind, M ;
Jorgensen, SB .
ENVIRONMENTAL MODELLING & SOFTWARE, 2004, 19 (09) :763-783