Evaluation of empirical formulae for estimation of the longitudinal dispersion in activated sludge reactors

被引:25
作者
Makinia, J
Wells, SA
机构
[1] Portland State Univ, Dept Civil & Environm Engn, Portland, OR 97207 USA
[2] Gdansk Tech Univ, Fac Civil & Environm Engn, PL-80952 Gdansk, Poland
关键词
activated sludge; dispersion; empirical formulae; mixing conditions; tracer studies;
D O I
10.1016/j.watres.2005.01.028
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Tracer studies are widely applied to characterize the hydraulic properties of reactors. In the case of activated sludge reactors, however, tracer test results are difficult to interpret due to internal and returned activated sludge recirculation. Empirical formulae can be considered as an alternative method of estimating the hydraulic conditions within the activated sludge reactor. The aim of this study is to evaluate accuracy of four empirical formulae for the full-scale conditions based on the results of tracer studies performed at the Rock Creek Wastewater Treatment Plant (WWTP) in Hillsboro, OR (USA). Values of the dispersion coefficient, E-L, were first estimated using a I-D advection-dispersion equation and setting a sum of squares of differences between the observed and calculated tracer concentrations to a minimum. The estimated values of EL coefficient remained within the range of 1043-1580 m(2)/h. The best approximation of dispersion was obtained from the formula of Fujie et al. (1983, J. Ferment. Technol. 63(3), 295). Also the formula of Murphy and Boyko (1970, J. San. Eng. ASCE 96(2), 211) generated EL values of the same order as the optimum EL. The accuracy of these formulae was further confirmed based on the results of studies reported in the literature. (c) 2005 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1533 / 1542
页数:10
相关论文
共 19 条
[1]   Model structure identification for wastewater treatment simulation based on computational fluid dynamics [J].
Alex, J ;
Kolisch, G ;
Krause, K .
WATER SCIENCE AND TECHNOLOGY, 2002, 45 (4-5) :325-334
[2]   OPTIMIZATION AND UPRATING OF ACTIVATED-SLUDGE PLANTS BY EFFICIENT PROCESS DESIGN [J].
CHAMBERS, B ;
JONES, GL .
WATER SCIENCE AND TECHNOLOGY, 1988, 20 (4-5) :121-132
[3]   Model-based characterisation of hydraulic, kinetic and influent properties of an industrial WWTP [J].
Coen, F ;
Petersen, B ;
Vanrolleghem, PA ;
Vanderhaegen, B ;
Henze, M .
WATER SCIENCE AND TECHNOLOGY, 1998, 37 (12) :317-326
[4]   Calibrating simple models for mixing and flow propagation in waste water treatment plants [J].
De Clercq, B ;
Coen, F ;
Vanderhaegen, B ;
Vanrolleghem, PA .
WATER SCIENCE AND TECHNOLOGY, 1999, 39 (04) :61-69
[5]  
ECKENFELDER WW, 1985, MATH MODELS BIOL WAS, V7, P95
[6]  
French RH, 1985, OPEN CHANNEL HYDRAUL
[7]  
FUJIE K, 1983, J FERMENT TECHNOL, V61, P295
[8]  
HARREMOES P, 1979, PROG WATER TECHNOL, V11, P49
[9]  
Horan N.J., 1990, Biological Wastewater Treatment Systems, Theory and Operation