Although many microfiltration membranes have asymmetric or composite struct
ures, there is little understanding of the effects of this multilayer struc
ture on fouling. A new model was developed that explicitly accounts for flu
id flow through two layers: an upper layer with noninterconnected pores and
a substructure with highly interconnected pores. Initial fouling occurs by
pore blockage, with a cake layer then forming over those regions covered b
y foulant. Model calculations are in excellent agreement with experimental
data for the filtrate flux and resistance during constant-pressure filtrati
on of bovine serum albumin. The highly interconnected pores within the supp
ort structure reduce the rate of flux decline by shunting more fluid throug
h the open pores. The extra resistance provided by the support also reduces
the relative importance of the protein deposit. The results provide import
ant insights into the effects of pore morphology on membrane fouling.