The cross-flow microfiltration flux is assumed to fall smoothly with a
decreasing slope from startup to the steady state. Under actual opera
ting conditions beyond a critical level, however, an anomalous decline
pattern arises; initially cross-flow medium filtration occurs and the
n thin-cake filtration. At the earlier stage, fine particles in polydi
spersed suspensoids are filtered out on the surface of the membrane an
d/or captured within the latter clogging the membrane pores gradually.
After the membrane surface is covered by the deposit, further filtrat
ion occurs by the buildup of filter cake on the initial deposit. Among
the many operating variables, three major controlling factors for the
earlier stage are confirmed: solids concentration, relative size of s
olids and pores, and relative force of sweeping and capturing of suspe
nsoids. Because suspended solids are separated by medium- and cake-law
filtration in a series a method for evaluating the time dependence of
flux with the new pattern is derived. Reliable flux analysis is achie
ved for the transient flux of the dilute suspension forming a low comp
ressibility fouling layer, which helps understand efficient flux perfo
rmance.