Permeation of binary gaseous mixtures through a silicalite-l membrane was s
tudied. Results are reported for the fluxes and separation factors as a fun
ction of the feed composition, the pressure and the temperature. For the va
rious cases a comparison is made between the binary and the single-componen
t permeation behavior. For the permeation of the mixtures the stronger adso
rbed component is little affected by the presence of the weaker adsorbed co
mponent. On the other hand for the weaker adsorbed component a clear reduct
ion in the flux is observed. As a consequence, the separation factor for mi
xtures differs considerably from the so-called ideal separation factor, whi
ch is the ratio of the one-component permeances. As expected, the separatio
n factor depends on the temperature. The separation factor is also a functi
on of the composition and the feed pressure. This means that the binary equ
ilibrium adsorption cannot be described with the extended Langmuir model. B
inary permeation and separation behavior is described using the ideal adsor
ption solution theory for equilibrium adsorption.