T. Matko et al., RECENT PROGRESS IN THE NUMERICAL MODELING OF WASTE-WATER SEDIMENTATION TANKS, Process safety and environmental protection, 74(B4), 1996, pp. 245-258
The recent progress in numerical modelling techniques applied to sedim
entation tanks in wastewater treatment is reviewed to determine their
usefulness. The models reviewed range from empirical models to sophist
icated computational fluid dynamics (CFD) models and the conclusions a
re as follows. Empirical models are still widely used today to predict
mainly the characteristics of the effluent and return sludge from sed
imentation tanks but cannot model the flow pattern or solids distribut
ion within the tank. The solids mass flux model is used to perform a m
ass balance on secondary sedimentation tanks for new designs or for th
e audit of a poor process and to determine the return sludge flow. It
can sometimes be used to monitor the height of the sludge blanket. The
lumped parameter model is usually used to determine the characteristi
cs of the effluent from primary sedimentation. CFD models are used to
predict the flow pattern and suspended solids distribution within the
tank and are normally applied in research to find the relationship bet
ween the tank hydraulics and process performance. Modelling using CFD
in the water industry has not been widespread because of the associate
d costs and the unfamiliarity with the mathematical models. The paper
suggests that the important CFD modelling criteria for the settling of
suspended solids in sedimentation tanks are the velocity distribution
, settling velocity distribution of suspended solids, turbulent mass d
iffusion of suspended solids, resuspension of settled solids from tank
base, temperature effects, flow variation, effect of flow on hoc grow
th or breakup, wind effects on the water surface and movement of scrap
ers. Gaps in the literature on CFD modelling can be identified for the
particle density, particle size, particle flocculation, the turbulent
mass diffusion of solids, the effect of the flow on particle growth o
r breakup, denitrification, wind on the water surface, baffle designs,
inlet pipe geometries, the side wall depth, the slope of the tank, th
e hopper design, peripheral weirs and in-board launders. Where possibl
e experimental data should be entered in these numerical models to giv
e realistic parameters and be used to validate these models.