An experimental study of the interaction of the enzyme yeast alcohol d
ehydrogenase (YADH) with polysulfone thin film composite microfiltrati
on membranes (Dow-Danmark) has been carried out. It was found that the
membranes adsorbed only approximately 3/4 of a monolayer of the enzym
e under the conditions studied. Even so, under filtration conditions,
the membrane permeation rate decreased continuously with time. This de
crease in permeation rate was due neither to concentration polarisatio
n nor to protein adsorption alone. However, it could be quantified usi
ng the standard blocking filtration law, which describes a decrease in
pore volume due to deposition of protein in the interior structure of
the membrane. Reversal of the membrane, so that the supporting matrix
faced the feed solution, gave more stable permeation rates. Implicati
ons for the microfiltration of industrial fermentation broths are disc
ussed.