Crossflow microfiltration is nor normally applied to mineral suspensio
n thickening and washing. However, its use is feasible and relatively
high filtrate flux rates can be achieved. Thus it may find application
for suspensions that are otherwise difficult to process such as clays
and slimes. A semi-empirical model of flux rate with the shear stress
on the deposit on the filter is shown to be applicable for the three
finely divided minerals investigated here. The model has been extended
to provide a relation for deposit depth with operating pressure. This
agreed with experimental data when filtering at pressures over I bar,
but needs to be developed further for operation at lower pressure. Th
ere are several operating modes that may be used for process operation
, the selection of the most appropriate one can be based on some simpl
e testwork to obtain the necessary empirical constants coupled with th
e design and operating equations derived from overall mass balances. T
he mass balances are based on the assumption that the crossflow system
can be treated as a well mixed tank. The experimental evidence sugges
ts that this is a reasonable assumption for both the thickening and di
afiltration studies reported here.