Details
| Original language | English |
|---|---|
| Pages (from-to) | 11-17 |
| Number of pages | 7 |
| Journal | Journal of membrane science |
| Volume | 329 |
| Issue number | 1-2 |
| Early online date | 30 Nov 2008 |
| Publication status | Published - 5 Mar 2009 |
Abstract
MFI membranes (ZSM-5 and silicalite-1) prepared by secondary growth on the core side of tubular titania supports, have been evaluated in the C4 olefin isomers separation under elevated pressure. The membranes were synthesized according to much simpler methods than described in literature for high flux membranes. The MFI membranes were tested under technical conditions with an undiluted 50%/50% 1-butene/i-butene feed up to 21 bar feed pressure without any sweep gas or reduced pressure on the permeate side at a temperature of 130 °C. With increasing pressure difference across the membrane, the permselectivity - formed as the ratio of the 1-butene and i-butene permeances in the binary mixture - was found to decrease from initially PS ≈ 20 at 2 bar pressure difference to about PS ≈ 2-3 at 20 bar pressure difference. Like the mixture permselectivity the mixture separation factor α - calculated from the 1-butene mole fraction in the feed and permeate - drops as well with increasing pressure difference from initially α ≈ 10 at 2 bar to about α ≈ 2-3 at 20 bar pressure difference. The reason for this loss in selectivity with increasing pressure is the decrease of the 1-butene permeance from initially about 4 m3(STP)m-2 h-1 bar-1 at Δp = 2 bar to less than 1 m3(STP)m-2 h-1 bar-1 at Δp = 20 bar. In contrast, the i-butene permeance is low but rather pressure-independent and remains therefore nearly constant. Both the curved adsorption isotherms and the reduced diffusivities for increased loadings are responsible for the less than linear increase of the 1-butene flux and the decreasing of the 1-butene permeances in the binary mixture with increasing pressure. The molecular reason for the decreasing 1-butene/i-butene selectivity with increasing pressure is the collapse of the 1-butene diffusivity in the presence of increasing amounts of co-adsorbed i-butene. This behavior shows that the separation of the C4 olefins follows not a simple molecular sieving mechanism but is based on the interplay of mixture adsorption and mixture diffusion.
Keywords
- Butene permeation, High pressure permeation, MFI membrane, Separation of butene isomers, Silicalite-1 membrane, Zeolite membrane, ZSM-5 membrane
ASJC Scopus subject areas
- Biochemistry, Genetics and Molecular Biology(all)
- Biochemistry
- Materials Science(all)
- Chemistry(all)
- Physical and Theoretical Chemistry
- Chemical Engineering(all)
- Filtration and Separation
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In: Journal of membrane science, Vol. 329, No. 1-2, 05.03.2009, p. 11-17.
Research output: Contribution to journal › Article › Research › peer review
}
TY - JOUR
T1 - Butene isomers separation on titania supported MFI membranes at conditions relevant for practice
AU - Voß, Hartwig
AU - Diefenbacher, Armin
AU - Schuch, Gunter
AU - Richter, Hannes
AU - Voigt, Ingolf
AU - Noack, Manfred
AU - Caro, Jürgen
PY - 2009/3/5
Y1 - 2009/3/5
N2 - MFI membranes (ZSM-5 and silicalite-1) prepared by secondary growth on the core side of tubular titania supports, have been evaluated in the C4 olefin isomers separation under elevated pressure. The membranes were synthesized according to much simpler methods than described in literature for high flux membranes. The MFI membranes were tested under technical conditions with an undiluted 50%/50% 1-butene/i-butene feed up to 21 bar feed pressure without any sweep gas or reduced pressure on the permeate side at a temperature of 130 °C. With increasing pressure difference across the membrane, the permselectivity - formed as the ratio of the 1-butene and i-butene permeances in the binary mixture - was found to decrease from initially PS ≈ 20 at 2 bar pressure difference to about PS ≈ 2-3 at 20 bar pressure difference. Like the mixture permselectivity the mixture separation factor α - calculated from the 1-butene mole fraction in the feed and permeate - drops as well with increasing pressure difference from initially α ≈ 10 at 2 bar to about α ≈ 2-3 at 20 bar pressure difference. The reason for this loss in selectivity with increasing pressure is the decrease of the 1-butene permeance from initially about 4 m3(STP)m-2 h-1 bar-1 at Δp = 2 bar to less than 1 m3(STP)m-2 h-1 bar-1 at Δp = 20 bar. In contrast, the i-butene permeance is low but rather pressure-independent and remains therefore nearly constant. Both the curved adsorption isotherms and the reduced diffusivities for increased loadings are responsible for the less than linear increase of the 1-butene flux and the decreasing of the 1-butene permeances in the binary mixture with increasing pressure. The molecular reason for the decreasing 1-butene/i-butene selectivity with increasing pressure is the collapse of the 1-butene diffusivity in the presence of increasing amounts of co-adsorbed i-butene. This behavior shows that the separation of the C4 olefins follows not a simple molecular sieving mechanism but is based on the interplay of mixture adsorption and mixture diffusion.
AB - MFI membranes (ZSM-5 and silicalite-1) prepared by secondary growth on the core side of tubular titania supports, have been evaluated in the C4 olefin isomers separation under elevated pressure. The membranes were synthesized according to much simpler methods than described in literature for high flux membranes. The MFI membranes were tested under technical conditions with an undiluted 50%/50% 1-butene/i-butene feed up to 21 bar feed pressure without any sweep gas or reduced pressure on the permeate side at a temperature of 130 °C. With increasing pressure difference across the membrane, the permselectivity - formed as the ratio of the 1-butene and i-butene permeances in the binary mixture - was found to decrease from initially PS ≈ 20 at 2 bar pressure difference to about PS ≈ 2-3 at 20 bar pressure difference. Like the mixture permselectivity the mixture separation factor α - calculated from the 1-butene mole fraction in the feed and permeate - drops as well with increasing pressure difference from initially α ≈ 10 at 2 bar to about α ≈ 2-3 at 20 bar pressure difference. The reason for this loss in selectivity with increasing pressure is the decrease of the 1-butene permeance from initially about 4 m3(STP)m-2 h-1 bar-1 at Δp = 2 bar to less than 1 m3(STP)m-2 h-1 bar-1 at Δp = 20 bar. In contrast, the i-butene permeance is low but rather pressure-independent and remains therefore nearly constant. Both the curved adsorption isotherms and the reduced diffusivities for increased loadings are responsible for the less than linear increase of the 1-butene flux and the decreasing of the 1-butene permeances in the binary mixture with increasing pressure. The molecular reason for the decreasing 1-butene/i-butene selectivity with increasing pressure is the collapse of the 1-butene diffusivity in the presence of increasing amounts of co-adsorbed i-butene. This behavior shows that the separation of the C4 olefins follows not a simple molecular sieving mechanism but is based on the interplay of mixture adsorption and mixture diffusion.
KW - Butene permeation
KW - High pressure permeation
KW - MFI membrane
KW - Separation of butene isomers
KW - Silicalite-1 membrane
KW - Zeolite membrane
KW - ZSM-5 membrane
UR - http://www.scopus.com/inward/record.url?scp=60049094845&partnerID=8YFLogxK
U2 - 10.1016/j.memsci.2008.11.039
DO - 10.1016/j.memsci.2008.11.039
M3 - Article
AN - SCOPUS:60049094845
VL - 329
SP - 11
EP - 17
JO - Journal of membrane science
JF - Journal of membrane science
SN - 0376-7388
IS - 1-2
ER -