Butene isomers separation on titania supported MFI membranes at conditions relevant for practice

authored by: Hartwig Voß, Armin Diefenbacher, Gunter Schuch, Hannes Richter, Ingolf Voigt, Manfred Noack, Jürgen Caro
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.
Organisation(s): Institute of Physical Chemistry and Electrochemistry
External Organisation(s): BASF SE
Fraunhofer Institute for Ceramic Technologies and Systems (IKTS)
University of Rostock
Type: Article
Journal: Journal of membrane science
Volume: 329
Pages: 11-17
No. of pages: 7
ISSN: 0376-7388
Publication date: 05.03.2009
Publication status: Published
Peer reviewed: Yes
ASJC Scopus subject areas: Biochemistry, Materials Science(all), Physical and Theoretical Chemistry, Filtration and Separation
Electronic version(s): https://doi.org/10.1016/j.memsci.2008.11.039 (Access: Closed)

BibTeX

@article{4648e88e3f214db487b8dad68fa773e6,
title = "Butene isomers separation on titania supported MFI membranes at conditions relevant for practice",
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",
author = "Hartwig Vo{\ss} and Armin Diefenbacher and Gunter Schuch and Hannes Richter and Ingolf Voigt and Manfred Noack and J{\"u}rgen Caro",
year = "2009",
month = mar,
day = "5",
doi = "10.1016/j.memsci.2008.11.039",
language = "English",
volume = "329",
pages = "11--17",
journal = "Journal of membrane science",
issn = "0376-7388",
publisher = "Elsevier",
number = "1-2",
}