The dehydration performance of a ceramic pervaporation membrane is studied
for the separation of isopropanol/water mixtures. The membranes are provide
d by ECN (The Netherlands) and consist of a water selective amorphous silic
a top layer and four alumina supporting layers. For the system investigated
, these membranes appear to combine high selectivities with high permeabili
ties. This results in a very high pervaporation separation index (PSI up to
6000 kg/m(2) h at 80 degreesC). A generalized Maxwell-Stefan model has bee
n set up to model the fluxes. From this analysis it follows, that the water
flux is only proportional to its own driving force. It is experimentally d
emonstrated that this holds for a wide range of operating conditions and fe
ed compositions. From these data, values of various Maxwell-Stefan diffusiv
ities are estimated. (C) 2001 Elsevier Science B.V. All rights reserved.