Abstract
The transport and separation of mixtures between benzene and p-xylene in pellets prepared by pressing of ZSM-5 powder and a dense supported (crystalline) Silicalite-1 membrane were compared to isolated ZSM-5 crystallites. The kinetics of the transport in the pressed pellet and the grown membrane determined in a Wicke-Kallenbach cell (313-403 K; partial pressure range 200-2300 Pa) differed significantly from those measured for isolated ZSM-5 particles with the pressure modulation frequency response technique (343-403 K; partial pressure 30 Pa). In a pressed pellet, the transport was of Knudsen type leading to high fluxes of 10-4 mol/m2 s and identical permeances for benzene and p-xylene. The diffusion coefficient in a pressed pellet exceeded that in particles, in which the transport was controlled by intracrystalline diffusion and the pore entrance step, by 8 orders of magnitude. The flux across a grown Silicalite-1 membrane was two orders of magnitude lower and the permeability of p-xylene was 2.6-5 times higher than that of benzene. The change in diffusivity in the membrane compared to the particles results from the higher surface coverage of p-xylene.
Original language | English |
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Pages (from-to) | 147-157 |
Number of pages | 11 |
Journal | Catalysis Today |
Volume | 168 |
Issue number | 1 |
DOIs | |
State | Published - 20 Jun 2011 |
Keywords
- Aromatic molecules
- Knudsen diffusion
- Pressure modulation frequency response
- Silicalite-1 membranes
- Stefan-Maxwell diffusion
- Wicke-Kallenbach experiments
- ZSM-5