Author(s)

M. Weiss, B. Gy. Plosz, K. Essemiani & J. Meinhold

Abstract

We present a CFD model that predicts the sedimentation of activated sludge in a full-scale circular secondary clarifier that is equipped with a suction-lift sludge removal system. The axisymmetric single-phase model is developed using the general-purpose CFD solver FLUENT 6, which uses the finite-volume method. A convection-diffusion equation, which is extended to incorporate the sedimentation of sludge flocs in the field of gravity, governs the mass transfer in the clarifier. The standard k- ε turbulence model is used to compute the turbulent motion, and our CFD model accounts for buoyancy flow and non-Newtonian flow behaviour of the mixed liquor. The activated sludge rheology was measured for varying sludge concentrations and temperatures. These measurements show that at shear rates typical of the flow in secondary clarifiers, the relationship between shear stress and shear rate follows the Casson law. The sludge settling velocity was measured as a function of the concentration, and we have used the double-exponential settling velocity function to describe its dependence on the concentration. The CFD model is validated using measured concentration profiles. Keywords: computational fluid dynamics, wastewater treatment, activated sludge, secondary clarifiers, sedimentation, rheology, suction-lift sludge removal. 1 Introduction Secondary clarifiers represent the final stage in the activated sludge wastewater treatment process, separating the treated water from the biologically active sludge (fig. 1). This solid/liquid separation is traditionally achieved by gravity sedimentation. These separation units, which act as clarifier, thickener, and storage tank, are often the major bottlenecks in the activated sludge process. Our

Keywords

computational fluid dynamics, wastewater treatment, activated sludge, secondary clarifiers, sedimentation, rheology, suction-lift sludge removal.