Ultrafiltration of river water for drinking water production was perfo
rmed with hollow fiber membranes in a crossflow filtration system with
frequent membrane backwashing. The effects of membrane material, oper
ating conditions and raw water quality on UF behavior were investigate
d. The permeate flux for the hydrophilic cellulose acetate (CA) membra
nes was much higher than that of the hydrophobic polyethersulfone (PES
) membrane, a phenomenon which was explained by membrane fouling due t
o the adsorption of substances in raw water on and in the pores of the
membranes. In order to maintain the high and stable flux for the CA m
embrane, the operating backwashing pressure should be more than twice
as high as the filtration pressure. It was also shown that efficient r
emoval of organic compounds from raw water was accomplished by the fou
led CA membrane.