One-dimensional modelling of the secondary clarifier-factors affecting simulation in the clarification zone and the assessment of the thickening flow dependence.

This paper presents a one-dimensional (1-D) model of the secondary settling tank (SST), and the drive for model development is discussed using steady-state simulation results generated with a 2-D computational fluid dynamics (CFD) model. Concentration profiles measured in a flat-bottom circular (fbSST) that is equipped with suction-lift sludge removal, served for CFD model validation. We investigate the factors that may deteriorate the 1-D simulation performance of clarifier models, which incorporate dispersion both in terms of the effluent sludge concentration and in terms of the sludge blanket height. Furthermore, dispersion-models can account for the effect of clarifier flow conditions on thickening performance. However, correlations, found in the literature, are shown to have limited efficiency under the wide flow boundary conditions examined in this study. Optimisation of the 1-D clarifier model structure is proposed by using an overflow dependent dispersion coefficient and including a feed flow dependent reduction factor in the downward convective velocity term. Results obtained show improved simulation performance in the clarification zone and allow for an efficient flow-dependency formulation of the thickening performance.

[1]  G. Ekama,et al.  Comparison of the 1D flux theory with a 2D hydrodynamic secondary settling tank model. , 2004, Water science and technology : a journal of the International Association on Water Pollution Research.

[2]  Ilse Smets,et al.  SENSITIVITY ANALYSIS OF A ONE-DIMENSIONAL CONVECTION-DIFFUSION MODEL FOR SECONDARY SETTLING TANKS , 2004 .

[3]  Sohrab Rohani,et al.  Dynamic and steady-state sedimentation of polydisperse suspension and prediction of outlets particle-size distribution , 2004 .

[4]  K. Essemiani,et al.  CFD modelling of sludge sedimentation in secondary clarifiers , 2006 .

[5]  Stefan Diehl,et al.  Operating charts for continuous sedimentation I: Control of steady states , 2001 .

[6]  Michael Knudson Stenstrom,et al.  A DYNAMIC MODEL AND COMPUTER COMPATIBLE CONTROL STRATEGIES FOR WASTEWATER TREATMENT PLANTS , 1976 .

[7]  Hans Vangheluwe,et al.  WEST: modelling biological wastewater treatment , 2003 .

[8]  P. Krebs,et al.  Denitrification in secondary clarifiers , 1995 .

[9]  I. Takács A dynamic model of the clarification-thickening process , 1991 .

[10]  W. Verstraete,et al.  On-line quantification of settling properties with in-sensor-experiments in an automated settlometer , 1996 .

[11]  Christopher G. Uchrin,et al.  Modeling and simulation of compressive gravity thickening of activated sludge , 1989 .

[12]  J. D. Clercq,et al.  Batch and continuous settling of activated sludge: in-depth monitoring and 1D compression modelling , 2006 .

[13]  Stefan Diehl,et al.  Operating Charts for Continuous Sedimentation II: Step Responses , 2005 .

[14]  P A Vanrolleghem,et al.  A new one-dimensional clarifier model--verification using full-scale experimental data. , 2003, Water science and technology : a journal of the International Association on Water Pollution Research.

[15]  Ulf Jeppsson,et al.  An evaluation of a dynamic model of the secondary clarifier , 1996 .

[16]  G. J. Kynch A theory of sedimentation , 1952 .

[17]  Raimund Bürger,et al.  On an extended clarifier-thickener model with singular source and sink terms , 2006 .

[18]  S. Svoronos,et al.  One-dimensional modeling of secondary clarifiers using a concentration and feed velocity-dependent dispersion coefficient , 1996 .

[19]  David Jenkins,et al.  Activated Sludge Separation Problems: Theory, Control Measures, Practical Experience , 2006 .

[20]  Benedek G. Plósz,et al.  Suction-lift sludge removal and non-Newtonian flow behaviour in circular secondary clarifiers: Numerical modelling and measurements , 2007 .

[21]  Ulf Jeppsson,et al.  A model of the settler coupled to the biological reactor , 1998 .

[22]  Peter Krebs Modellierung und Verbesserung der Strömung in Nachklärbecken , 1991 .

[23]  Raimund Bürger,et al.  A Model of Continuous Sedimentation of Flocculated Suspensions in Clarifier-Thickener Units , 2005, SIAM J. Appl. Math..

[24]  Stefan Diehl,et al.  Operating Charts for Continuous Sedimentation III: Control of Step Inputs , 2006 .

[25]  D. S. Parker,et al.  REVIEW OF FOLKLORE IN DESIGN AND OPERATION OF SECONDARY CLARIFIERS , 2001 .

[26]  John A. Nelder,et al.  A Simplex Method for Function Minimization , 1965, Comput. J..