Flocculant addition caused an increase in the permeate flux and a decrease in the specific cake resistance in dead-end microfiltration. Structural differences in the cakes that may have accounted for the flux differences were examined by light microscopy. Flux improvements did not fully carry over to stirred-cell and crossflow experiments and measurement of floc size distributions showed that floc breakup may have been one cause for this. Additional experiments were conducted to determine the effect of flocculant dose on floc stability under shear.