Details
| Original language | English |
|---|---|
| Pages (from-to) | 27-36 |
| Number of pages | 10 |
| Journal | Microporous and Mesoporous Materials |
| Volume | 54 |
| Issue number | 1-2 |
| Early online date | 3 May 2002 |
| Publication status | Published - 1 Jul 2002 |
| Externally published | Yes |
Abstract
Composite membranes that consist of thin faujasite layers on the surfaces of porous α-Al2O3 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 μm 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 H2 > CH4 > N2 > O2 > CO2 > nC4H10 > SF6 at 23 °C. The separation factors α of equimolar binary gas mixtures were measured at 23°C. For the gas mixture N2/ CO2 an α of 8.4 was found, for the mixture CH4/CO2 α 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.
Keywords
- FAU membrane, Gas mixture separation, Membrane preparation, Molecular sieve, Single-gas permeation
ASJC Scopus subject areas
- Chemistry(all)
- General Chemistry
- Materials Science(all)
- General Materials Science
- Physics and Astronomy(all)
- Condensed Matter Physics
- Engineering(all)
- Mechanics of Materials
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In: Microporous and Mesoporous Materials, Vol. 54, No. 1-2, 01.07.2002, p. 27-36.
Research output: Contribution to journal › Article › Research › peer review
}
TY - JOUR
T1 - Permeation of single gases and gas mixtures through faujasite-type molecular sieve membranes
AU - Weh, K.
AU - Noack, M.
AU - Sieber, I.
AU - Caro, J.
PY - 2002/7/1
Y1 - 2002/7/1
N2 - Composite membranes that consist of thin faujasite layers on the surfaces of porous α-Al2O3 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 μm 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 H2 > CH4 > N2 > O2 > CO2 > nC4H10 > SF6 at 23 °C. The separation factors α of equimolar binary gas mixtures were measured at 23°C. For the gas mixture N2/ CO2 an α of 8.4 was found, for the mixture CH4/CO2 α 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.
AB - Composite membranes that consist of thin faujasite layers on the surfaces of porous α-Al2O3 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 μm 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 H2 > CH4 > N2 > O2 > CO2 > nC4H10 > SF6 at 23 °C. The separation factors α of equimolar binary gas mixtures were measured at 23°C. For the gas mixture N2/ CO2 an α of 8.4 was found, for the mixture CH4/CO2 α 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.
KW - FAU membrane
KW - Gas mixture separation
KW - Membrane preparation
KW - Molecular sieve
KW - Single-gas permeation
UR - http://www.scopus.com/inward/record.url?scp=0036629083&partnerID=8YFLogxK
U2 - 10.1016/S1387-1811(02)00381-5
DO - 10.1016/S1387-1811(02)00381-5
M3 - Article
AN - SCOPUS:0036629083
VL - 54
SP - 27
EP - 36
JO - Microporous and Mesoporous Materials
JF - Microporous and Mesoporous Materials
SN - 1387-1811
IS - 1-2
ER -