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Permeation of single gases and gas mixtures through faujasite-type molecular sieve membranes

✍ Scribed by K. Weh; M. Noack; I. Sieber; J. Caro


Book ID
104430691
Publisher
Elsevier Science
Year
2002
Tongue
English
Weight
414 KB
Volume
54
Category
Article
ISSN
1387-1811

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✦ Synopsis


Composite membranes that consist of thin faujasite layers on the surfaces of porous a-Al 2 O 3 support disks were prepared by using a two-step synthesis. First, a seed layer of externally synthesized Na-Y nanocrystals was deposited on the surface of the support. Second, the polycrystalline faujasite layer was grown hydrothermally. Characterization by X-ray diffraction, field emission-scanning electron microscopy and energy dispersive X-ray spectroscopy showed dense intergrown FAU layers with Si/Al ratios of 1.3-1.8 and layer thicknesses in the range of 0.8-6 lm depending on the synthesis conditions. Two different kinds of heating were used in the second synthesis step, either a conventional oven or a microwave oven. The synthesis conditions like crystallization time and temperature as well as the kind of heating influenced the permeation properties of the supported faujasite membranes. The thicker the FAU layers, the lower were the permeances of the single gases which were found to be of the order H 2 > CH 4 > N 2 > O 2 > CO 2 > nC 4 H 10 > SF 6 at 23 Β°C. The separation factors a of equimolar binary gas mixtures were measured at 23 Β°C. For the gas mixture N 2 / CO 2 an a of 8.4 was found, for the mixture CH 4 /CO 2 a was 3.5. From these permeation characteristics one can draw the conclusion that the separation of these small gas molecules by the large and heteropolar FAU (Na-X) pore system with 0.74 nm pore opening diameters is mainly based on differences of adsorption or diffusion rates, rather than on size exclusion like in LTA-or MFI-type zeolite membranes.


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A β€œfree volume” model of permeation of g
✍ S.-M. Fang; S.A. Stern; H.L. Frisch πŸ“‚ Article πŸ“… 1975 πŸ› Elsevier Science 🌐 English βš– 801 KB

A recent "free volume" model of gas permeation (3) has been extended to the transport of gas mixtures through nonporous polymeric membranes. The present model assumes that the rates of transport of the components of a mixture depend on the free volume of the gas-polymer system, and that the effect o