Membranes containing selective fillers, such as zeolites and activated
carbon, can improve the separation by pervaporation. Applications of
adsorbent-filled membranes in pervaporation have been demonstrated by
a number of studies. These applications include removal of organic com
pounds from water, dehydration of azeotropic mixtures, and organic/org
anic separation. Three different types of adsorbents have been evaluat
ed: zeolites, activated carbon, and carbon molecular sieves. Experimen
tal results show the most promising filled membrane is the silicalite-
filled poly(dimethylsiloxane) (PDMS) membrane which can be effectively
used in the removal of organic compounds from water. The transport of
species through adsorbent-filled membranes occurs by a sorption-diffu
sion mechanism. Sorption of species in the filled rubbery membranes ca
n be described by a dual sorption model. Modeling of the transport pro
cess through filled membranes involves mass-transfer resistances in th
e different phases of the membranes: in the polymer phase, in the adso
rbent phase, and in a polymer-adsorbent interface. Several models base
d on resistance-in-series mechanisms that were developed to describe t
he experimental results were reviewed.