R. Krishna et Ljp. Vandenbroeke, THE MAXWELL-STEFAN DESCRIPTION OF MASS-TRANSPORT ACROSS ZEOLITE MEMBRANES, Chemical engineering journal and the biochemical engineering journal, 57(2), 1995, pp. 155-162
Published experimental data on transient permeation fluxes of light hy
drocarbons through a silicalite-1 membrane show curious behaviour. For
a mixture of methane and n-butane, for example, the transient experim
ents showed that initially the permeation flux of methane is higher th
an for n-butane but that this methane flux reduces to a lower steady s
tate value. The n-butane flux is initially low but under steady state
conditions is much higher than that for methane. A mathematical model
for transient membrane mass transport has been developed using the Max
well-Stefan formulation. This model is able to predict the observed ma
ximum in the flux of methane, and if we assume that the Fick diffusivi
ty is constant the transient permeation fluxes are predicted to reach
their steady state values monotonically. Thus the Pick formulation fai
ls even at the qualitative level to explain the experimental results.
It is concluded that the Maxwell-Stefan formulation is indispensable f
or the description of mass transport across zeolite membranes.