The loss of membrane flux due to fouling is one of the main impediment
s in the development of membrane processes for use in drinking water t
reatment. The objective of this work was to determine the nature of na
nofiltration membrane foulants for a pilot system fed conventionally t
reated Ohio River water for 15 months. The foulant responsible for flu
x loss was shown to be a film layer 20-80 mu m thick with the greatest
depth in the first of three elements in series. Heterotrophic plate c
ount, phospholipid, and pyrolysis-GC/MS analyses showed the film layer
had a strong biological signature. The inorganic contribution to the
dried film layer was low (less than 15%). Both acid and alkaline/deter
gent cleaning yielded only short-term flux recovery, although they wer
e independent of each other. Neither acid cleaning, alkaline/detergent
cleaning, nor hydraulic flushing removed the thickness of the film la
yer, nor changed its organic characteristics. Only alkaline/detergent
cleaning inactivated a large percentage of the film-layer microbes. Th
e short-term flux recovery without loss of biofilm thickness suggests
a morphological change upon chemical cleaning. The results suggest tha
t feedwater pretreatment to prevent cell deposition and subsequent bio
growth would he more successful than chemical cleaning the membrane af
ter biofouling.