Continuous Separation of Light Olefin/Paraffin Mixtures on ZIF-4 by Pressure Swing Adsorption and Membrane Permeation

In this study, two zeolitic imidazolate frameworks (ZIFs) called ZIF-4 and ZIF-zni (zni is the network topology) were characterized by sorption studies regarding their paraffin/olefin separation potential. In particular, equilibrated pure and mixed gas adsorption isotherms of ethane and ethene were...

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Main Authors: Maximilian Hovestadt, Sebastian Friebe, Lailah Helmich, Marcus Lange, Jens Möllmer, Roger Gläser, Alexander Mundstock, Martin Hartmann
Format: Article
Language:English
Published: MDPI AG 2018-04-01
Series:Molecules
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Online Access:http://www.mdpi.com/1420-3049/23/4/889
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author Maximilian Hovestadt
Sebastian Friebe
Lailah Helmich
Marcus Lange
Jens Möllmer
Roger Gläser
Alexander Mundstock
Martin Hartmann
author_facet Maximilian Hovestadt
Sebastian Friebe
Lailah Helmich
Marcus Lange
Jens Möllmer
Roger Gläser
Alexander Mundstock
Martin Hartmann
author_sort Maximilian Hovestadt
collection DOAJ
description In this study, two zeolitic imidazolate frameworks (ZIFs) called ZIF-4 and ZIF-zni (zni is the network topology) were characterized by sorption studies regarding their paraffin/olefin separation potential. In particular, equilibrated pure and mixed gas adsorption isotherms of ethane and ethene were recorded at 293 K up to 3 MPa. ZIF-4 exhibits selectivities for ethane in the range of 1.5–3, which is promising for continuous pressure swing adsorption (PSA). ZIF-4 shows high cycle stability with promising separation potential regarding ethane, which results in purification of the more industrial desired olefin. Furthermore, both ZIF materials were implemented in Matrimid to prepare a mixed matrix membrane (MMM) and were used in the continuous separation of a propane/propene mixture. The separation performance of the neat polymer is drastically increased after embedding porous ZIF-4 crystals in the Matrimid matrix, especially at higher feed pressures (3–5 barg). Due to the smaller kinetic diameter of the olefin, the permeability is higher compared to the paraffin.
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spelling doaj.art-7308a7d5edd94783a73e2eb47db5689b2022-12-22T03:42:00ZengMDPI AGMolecules1420-30492018-04-0123488910.3390/molecules23040889molecules23040889Continuous Separation of Light Olefin/Paraffin Mixtures on ZIF-4 by Pressure Swing Adsorption and Membrane PermeationMaximilian Hovestadt0Sebastian Friebe1Lailah Helmich2Marcus Lange3Jens Möllmer4Roger Gläser5Alexander Mundstock6Martin Hartmann7Erlangen Catalysis Resource Center (ECRC), Friedrich-Alexander-Universität Erlangen-Nürnberg (FAU), Egerlandstr. 3, 91058 Erlangen, GermanyInstitute of Physical Chemistry and Electrochemistry, Leibniz University Hannover, Callinstrasse 3A, 30167 Hannover, GermanyInstitute of Physical Chemistry and Electrochemistry, Leibniz University Hannover, Callinstrasse 3A, 30167 Hannover, GermanyInstitut für Nichtklassische Chemie e.V. (INC), Permoserstraße 15, 04318 Leipzig, GermanyInstitut für Nichtklassische Chemie e.V. (INC), Permoserstraße 15, 04318 Leipzig, GermanyInstitut für Nichtklassische Chemie e.V. (INC), Permoserstraße 15, 04318 Leipzig, GermanyInstitute of Physical Chemistry and Electrochemistry, Leibniz University Hannover, Callinstrasse 3A, 30167 Hannover, GermanyErlangen Catalysis Resource Center (ECRC), Friedrich-Alexander-Universität Erlangen-Nürnberg (FAU), Egerlandstr. 3, 91058 Erlangen, GermanyIn this study, two zeolitic imidazolate frameworks (ZIFs) called ZIF-4 and ZIF-zni (zni is the network topology) were characterized by sorption studies regarding their paraffin/olefin separation potential. In particular, equilibrated pure and mixed gas adsorption isotherms of ethane and ethene were recorded at 293 K up to 3 MPa. ZIF-4 exhibits selectivities for ethane in the range of 1.5–3, which is promising for continuous pressure swing adsorption (PSA). ZIF-4 shows high cycle stability with promising separation potential regarding ethane, which results in purification of the more industrial desired olefin. Furthermore, both ZIF materials were implemented in Matrimid to prepare a mixed matrix membrane (MMM) and were used in the continuous separation of a propane/propene mixture. The separation performance of the neat polymer is drastically increased after embedding porous ZIF-4 crystals in the Matrimid matrix, especially at higher feed pressures (3–5 barg). Due to the smaller kinetic diameter of the olefin, the permeability is higher compared to the paraffin.http://www.mdpi.com/1420-3049/23/4/889ZIF-4olefin/paraffin separationpressure swing adsorption (PSA)membrane permeation
spellingShingle Maximilian Hovestadt
Sebastian Friebe
Lailah Helmich
Marcus Lange
Jens Möllmer
Roger Gläser
Alexander Mundstock
Martin Hartmann
Continuous Separation of Light Olefin/Paraffin Mixtures on ZIF-4 by Pressure Swing Adsorption and Membrane Permeation
Molecules
ZIF-4
olefin/paraffin separation
pressure swing adsorption (PSA)
membrane permeation
title Continuous Separation of Light Olefin/Paraffin Mixtures on ZIF-4 by Pressure Swing Adsorption and Membrane Permeation
title_full Continuous Separation of Light Olefin/Paraffin Mixtures on ZIF-4 by Pressure Swing Adsorption and Membrane Permeation
title_fullStr Continuous Separation of Light Olefin/Paraffin Mixtures on ZIF-4 by Pressure Swing Adsorption and Membrane Permeation
title_full_unstemmed Continuous Separation of Light Olefin/Paraffin Mixtures on ZIF-4 by Pressure Swing Adsorption and Membrane Permeation
title_short Continuous Separation of Light Olefin/Paraffin Mixtures on ZIF-4 by Pressure Swing Adsorption and Membrane Permeation
title_sort continuous separation of light olefin paraffin mixtures on zif 4 by pressure swing adsorption and membrane permeation
topic ZIF-4
olefin/paraffin separation
pressure swing adsorption (PSA)
membrane permeation
url http://www.mdpi.com/1420-3049/23/4/889
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