Filtration is an important solid-liquid separation technology employed wide
ly in the mineral processing industries. The effectiveness of the filtratio
n operation can be influenced by numerous variables, related to the particu
late phase, the slurry rheology and the equipment. Continuous filtration of
fine particles involves filter cake formation and removal of surface moist
ure by drawing air through the pore structure network. In order to gain a b
etter understanding of the complex transport phenomena that occur in the fi
lter cake, analysis of the effect of the three-dimensional pore geometry on
the effective transport properties of the filter cake is necessary. In thi
s regard, analysis of the pore connectivity in a packed bed of particles sh
ould allow for a detailed description of fluid flow and transport in the fi
lter cake structure. Two interrelated approaches, namely computer simulatio
n and experimental measurement, can be used to gain knowledge of pore micro
structure and its correlation to macroscopic cake properties. In this regar
d, a three-dimensional Monte Carlo method was used in this work to simulate
cake structure. As the resolution and the techniques for three-dimensional
geometric analysis have advanced in the last decade, experimental measurem
ents are now possible to specify in detail the pore structure in three-dime
nsional digital space using high-resolution X-ray microtomography. Thus in
addition to computer simulation, this paper presents preliminary experiment
al findings of pore structure in three-dimensional using X-ray microtomogra
phic techniques. These experimental results are contrasted to results from
computer simulation. (C) 2000 Elsevier Science B.V. All rights reserved.