Full-scale modelling of an ozone reactor for drinking water treatment

被引:54
作者
Audenaert, Wim T. M. [1 ,2 ]
Callewaert, Manly [2 ]
Nopens, Ingmar [1 ]
Cromphout, Jan [3 ]
Vanhoucke, Robert [3 ]
Dumoulin, Ann [2 ]
Dejans, Pascal [2 ]
Van Hulle, Stijn W. H. [1 ,2 ]
机构
[1] Univ Ghent, Dept Appl Math Biometr & Proc Control, BIOMATH, B-9000 Ghent, Belgium
[2] Univ Coll W Flanders, Dept Ind Engn & Technol, EnBiChem Res Grp, B-8500 Kortrijk, Belgium
[3] Flemish Water Supply Co, VMW, B-1040 Brussels, Belgium
关键词
Advanced oxidation processes; Ozone; Kinetic model; Organic contaminant; Full-scale drinking water production; BROMIDE-CONTAINING WATERS; HYDROGEN-PEROXIDE; PULSE-RADIOLYSIS; KINETIC-MODEL; DECOMPOSITION; OZONATION; DISINFECTION;
D O I
10.1016/j.cej.2009.12.051
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
In 2003, the Flemish Water Supply Company (VMW) extended its drinking water production site in Kluizen (near Ghent, Belgium) with a combined ozonation and biological granular activated carbon (BGAC) filtration process. Due to this upgrade, biostability increased, less chlorination was needed and drinking water quality improved significantly. The aim of this study was to describe the full-scale reactor with a limited set of equations. In order to describe the ozonation process, a model including key processes such as ozone decomposition, organic carbon removal, disinfection and bromate formation was developed. Kinetics were implemented in WEST (R) and simulation results were compared to real data. The predicting performance was verified with a goodness-of-fit test and key parameters were determined through a local sensitivity analysis. Parameters involving optical density (both rate constants and stoichiometric coefficients) strongly affect model output. Some parameters with respect to bromate and bacteria showed to be only, but to a large extent, sensitive to their associated concentrations. A scenario analysis was performed to study the system's behavior at different operational conditions. It was demonstrated that the model is able to describe the operation of the full-scale ozone reactor, however, further data collection for model validation is necessary. (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:551 / 557
页数:7
相关论文
共 35 条
[1]  
American Public Health Association, 1992, STAND METH EX WAT WA
[2]  
[Anonymous], THESIS DELFT U TECHN
[3]   DETERMINATION OF OZONE IN WATER BY THE INDIGO METHOD [J].
BADER, H ;
HOIGNE, J .
WATER RESEARCH, 1981, 15 (04) :449-456
[4]  
Beltran J.F., 2004, OZONE REACTION KINET
[5]  
BOUCHERIE C, 2009, CUTEC PUBLICATION SE
[6]  
BUHLER RE, 1984, J PHYS CHEM-US, V88, P2560
[7]  
Crittenden J.C., 2005, Water treatment principles and design
[8]  
CROMPHOUT J, 2005, TRIBUNE EAU, V58, P15
[9]  
CROMPHOUT J, 2008, P 10A EA3G VIVAQUA I
[10]   Practical aspects of sensitivity function approximation for dynamic models [J].
De Pauw, Dirk J. W. ;
Vanrolleghem, Peter A. .
MATHEMATICAL AND COMPUTER MODELLING OF DYNAMICAL SYSTEMS, 2006, 12 (05) :395-414