This paper describes the calibration and the verification of the previ
ously proposed filtration model (UF model) with several sets of experi
mental data obtained with various operating conditions using alum floc
s. The model was improved by including a simplified interpore floccula
tion equation that deals with the growth of flocs flowing through filt
er pore channels, in order to compensate for differences between calcu
lated and experimental results in a deeper bed. The improved filtratio
n model (UF-PF model) successfully describes a breakthrough curve and
a head loss buildup of the filtration process, The variations of remov
al efficiency and head loss during the filtration process, for various
sand grain sizes, filtration velocities, and depths of filter bed, ca
n be predicted by means of numerical simulations of the proposed filtr
ation equations with the parameters relating to flee properties, The o
ptimum operational design which provides a maximum filtrate production
during a filter run and its search algorithms, is also discussed for
uniform and dual layer fillers by using numerical simulations of the U
F-PF model. The design variables considered are grain sizes, filter la
yer depths and flow rates,