The membrane extraction experiments were performed with tributyl phosphate/
acetic acid (HAc)/water, n-butanol/HAc/water and 20% Alamine (in kerosene);
HAc; and water as working systems. HAc was transferred from the aqueous ph
ase to the organic phase. The effect of flat membranes swelling on mass tra
nsfer was studied. The membranes were microporous polysulfone and microporo
us polytetrafluoroethylene. The overall mass transfer coefficients based on
the water phase were calculated and compared between nonswollen and swolle
n membranes. The experimental results show that the physical structure of t
he flat membranes used in our experiments was changed if soaked by organic
solvents; however, change in thickness was not found. The overall mass tran
sfer coefficients clearly were decreased after the flat membranes were swol
len. The most likely reason is that the mass transfer resistance was increa
sed because of the change of the membrane structure. The results also show
that it is better to choose a hydrophilic membrane to reach high mass trans
fer performance when the equilibrium constant is very low. (C) 1999 John Wi
ley & Sons, Inc.