Biological nutrient removal model No.1 (BNRM1)

被引:41
作者
Seco, A
Ribes, J
Serralta, J
Ferrer, J
机构
[1] Univ Valencia, Dpto Ingn Quim, E-46100 Burjassot, Spain
[2] Univ Politecn Valencia, Dpto Ingn Hidraul & Medio Ambiente, Valencia 46022, Spain
关键词
anaerobic digestion; biological nutrient removal; chemical model; mathematical modelling; settling model; WWTP simulation;
D O I
10.2166/wst.2004.0361
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This paper presents the results of the work carried out by the CALAGUA Group on Mathematical Modelling of Biological Treatment Processes: the Biological Nutrient Removal Model No. 1. This model is based on a new concept for dynamic simulation of wastewater treatment plants: a unique model can be used to design, simulate and optimize the whole plant, as it includes most of the biological and physico-chemical processes taking place in all treatment operations. The physical processes included are: settling and clarification processes (flocculated settling, hindered settling and thickening), volatile fatty acids elutriation and gas-liquid transfer. The chemical interactions included comprise acid-base processes, where equilibrium conditions are assumed. The biological processes included are: organic matter, nitrogen and phosphorus removal; acidogenesis, acetogenesis and methanogenesis. Environmental conditions in each operation unit (aerobic, anoxic or anaerobic) will determine which bacterial groups can grow. Thus, only the model parameters related to bacterial groups able to grow in any of the operation units of a specific WWTP will require calibration. One of the most important advantages of this model is that no additional analysis with respect to ASM2d is required for wastewater characterization. Some applications of this model have also been briefly explained in this paper.
引用
收藏
页码:69 / 78
页数:10
相关论文
共 9 条
[1]  
BATSTONE DJ, 2002, 13 SCI TECHN
[2]   Calibration and simulation of two large wastewater treatment plants operated for nutrient removal [J].
Ferrer, J ;
Morenilla, JJ ;
Bouzas, A ;
García-Usach, F .
WATER SCIENCE AND TECHNOLOGY, 2004, 50 (06) :87-94
[3]   Activated Sludge Model No.2d, ASM2d [J].
Henze, M ;
Gujer, W ;
Mino, T ;
Matsuo, T ;
Wentzel, MC ;
Marais, GVR ;
Van Loosdrecht, MCM .
WATER SCIENCE AND TECHNOLOGY, 1999, 39 (01) :165-182
[4]   Modelling of an activated primary settling tank including the fermentation process and VFA elutriation [J].
Ribes, J ;
Ferrer, J ;
Bouzas, A ;
Seco, A .
ENVIRONMENTAL TECHNOLOGY, 2002, 23 (10) :1147-1156
[5]   Calibration of kinetic parameters in the IAWQ Activated Sludge Model: a pilot scale experience [J].
Satoh, H ;
Okuda, E ;
Mino, T ;
Matsuo, T .
WATER SCIENCE AND TECHNOLOGY, 2000, 42 (3-4) :29-34
[6]  
SECO A, 2003, P 9 C DES OP COSTS L
[7]   A supervisory control system for optimising nitrogen removal and aeration energy consumption in wastewater treatment plants [J].
Serralta, J ;
Ribes, J ;
Seco, A ;
Ferrer, J .
WATER SCIENCE AND TECHNOLOGY, 2002, 45 (4-5) :309-316
[8]  
SERRALTA J, 2003, UNPUB WATER RES
[9]   A DYNAMIC-MODEL OF THE CLARIFICATION THICKENING PROCESS [J].
TAKACS, I ;
PATRY, GG ;
NOLASCO, D .
WATER RESEARCH, 1991, 25 (10) :1263-1271