In wastewater treatment, oxidation ditches are used for the removal of carb
on and nitrogen of activated sludge. The control of the single-phase flow i
s essential to the optimisation of the whole process. Among the two global
functioning parameters (mean liquid velocity U-c, power dissipated per unit
of volume P/V), the mean circulation velocity can be recommended. Indeed,
the values of the power dissipated per unit of volume P/V obtained in diffe
rent scale plant show that the industrial criterion on P/V leads to an over
design of channel. Therefore a mean liquid circulation velocity U-c created
by horizontal impellers must be maintained inside the ditch. In order to p
redict the velocity U-c, a model has been proposed based on the Equations o
f the continuity and motion and using a few simple parameters. Experiments
were carried out on pilot plant (1m(3)) and full scale ditches (860, 1400 a
nd 2800m(3)) in which the characteristics of the mixing system and the dime
nsions of channels were varied. A good agreement was observed between the m
odel predictions and experimental data for the mean circulation velocity U-
c.