Comparative permeation studies on three supported membranes: Pure ZIF-8, pure polymethylphenylsiloxane, and mixed matrix membranes

Publikation: Beitrag in FachzeitschriftArtikelForschungPeer-Review

Autorschaft

  • L. Diestel
  • X. L. Liu
  • Y. S. Li
  • W. S. Yang
  • J. Caro

Externe Organisationen

  • CAS - Dalian Institute of Chemical Physics
Forschungs-netzwerk anzeigen

Details

OriginalspracheEnglisch
Seiten (von - bis)210-215
Seitenumfang6
FachzeitschriftMicroporous and Mesoporous Materials
Jahrgang189
Frühes Online-Datum21 Sept. 2013
PublikationsstatusVeröffentlicht - 1 Mai 2014

Abstract

We studied the separation of four practice-relevant gas mixtures on three different membranes which were prepared on porous alumina supports: (i) a pure ZIF-8 (zeolitic imidazolate framework), (ii) a pure PMPS (polymethylphenylsiloxane) polymer, and (iii) a mixed matrix membrane (MMM, with 8.3 wt.% ≈ 8.8 vol.% ZIF-8 (density 0.93 g cm-3) in PMPS (density 1.00 g cm-3)). The four gas mixtures under study were: CO 2/CH4, CO2/N2, H2/CO 2, and O2/N2. Whereas the pure ZIF-8 membrane shows the best separation factor α = 11 for H2/CH4, the pure PMPS membrane has higher separation factors for the CO2 separation from other gases. It was anticipated that the separation behavior of the MMM results from an interplay of the permeation through the PMPS polymer matrix and the embedded ZIF-8 nanocrystals. Actually, the separation factors of the MMM were found to be equal to the separation factors of the pure polymer membrane. However, we measured much higher gas fluxes through the MMM than through the pure polymer membrane. This experimental finding could indicate an increase of the free volume of the PMPS polymer after introduction of ZIF-8 nanoparticles.

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Comparative permeation studies on three supported membranes: Pure ZIF-8, pure polymethylphenylsiloxane, and mixed matrix membranes. / Diestel, L.; Liu, X. L.; Li, Y. S. et al.
in: Microporous and Mesoporous Materials, Jahrgang 189, 01.05.2014, S. 210-215.

Publikation: Beitrag in FachzeitschriftArtikelForschungPeer-Review

Diestel L, Liu XL, Li YS, Yang WS, Caro J. Comparative permeation studies on three supported membranes: Pure ZIF-8, pure polymethylphenylsiloxane, and mixed matrix membranes. Microporous and Mesoporous Materials. 2014 Mai 1;189:210-215. Epub 2013 Sep 21. doi: 10.1016/j.micromeso.2013.09.012
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abstract = "We studied the separation of four practice-relevant gas mixtures on three different membranes which were prepared on porous alumina supports: (i) a pure ZIF-8 (zeolitic imidazolate framework), (ii) a pure PMPS (polymethylphenylsiloxane) polymer, and (iii) a mixed matrix membrane (MMM, with 8.3 wt.% ≈ 8.8 vol.% ZIF-8 (density 0.93 g cm-3) in PMPS (density 1.00 g cm-3)). The four gas mixtures under study were: CO 2/CH4, CO2/N2, H2/CO 2, and O2/N2. Whereas the pure ZIF-8 membrane shows the best separation factor α = 11 for H2/CH4, the pure PMPS membrane has higher separation factors for the CO2 separation from other gases. It was anticipated that the separation behavior of the MMM results from an interplay of the permeation through the PMPS polymer matrix and the embedded ZIF-8 nanocrystals. Actually, the separation factors of the MMM were found to be equal to the separation factors of the pure polymer membrane. However, we measured much higher gas fluxes through the MMM than through the pure polymer membrane. This experimental finding could indicate an increase of the free volume of the PMPS polymer after introduction of ZIF-8 nanoparticles.",
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Download

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T1 - Comparative permeation studies on three supported membranes

T2 - Pure ZIF-8, pure polymethylphenylsiloxane, and mixed matrix membranes

AU - Diestel, L.

AU - Liu, X. L.

AU - Li, Y. S.

AU - Yang, W. S.

AU - Caro, J.

PY - 2014/5/1

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N2 - We studied the separation of four practice-relevant gas mixtures on three different membranes which were prepared on porous alumina supports: (i) a pure ZIF-8 (zeolitic imidazolate framework), (ii) a pure PMPS (polymethylphenylsiloxane) polymer, and (iii) a mixed matrix membrane (MMM, with 8.3 wt.% ≈ 8.8 vol.% ZIF-8 (density 0.93 g cm-3) in PMPS (density 1.00 g cm-3)). The four gas mixtures under study were: CO 2/CH4, CO2/N2, H2/CO 2, and O2/N2. Whereas the pure ZIF-8 membrane shows the best separation factor α = 11 for H2/CH4, the pure PMPS membrane has higher separation factors for the CO2 separation from other gases. It was anticipated that the separation behavior of the MMM results from an interplay of the permeation through the PMPS polymer matrix and the embedded ZIF-8 nanocrystals. Actually, the separation factors of the MMM were found to be equal to the separation factors of the pure polymer membrane. However, we measured much higher gas fluxes through the MMM than through the pure polymer membrane. This experimental finding could indicate an increase of the free volume of the PMPS polymer after introduction of ZIF-8 nanoparticles.

AB - We studied the separation of four practice-relevant gas mixtures on three different membranes which were prepared on porous alumina supports: (i) a pure ZIF-8 (zeolitic imidazolate framework), (ii) a pure PMPS (polymethylphenylsiloxane) polymer, and (iii) a mixed matrix membrane (MMM, with 8.3 wt.% ≈ 8.8 vol.% ZIF-8 (density 0.93 g cm-3) in PMPS (density 1.00 g cm-3)). The four gas mixtures under study were: CO 2/CH4, CO2/N2, H2/CO 2, and O2/N2. Whereas the pure ZIF-8 membrane shows the best separation factor α = 11 for H2/CH4, the pure PMPS membrane has higher separation factors for the CO2 separation from other gases. It was anticipated that the separation behavior of the MMM results from an interplay of the permeation through the PMPS polymer matrix and the embedded ZIF-8 nanocrystals. Actually, the separation factors of the MMM were found to be equal to the separation factors of the pure polymer membrane. However, we measured much higher gas fluxes through the MMM than through the pure polymer membrane. This experimental finding could indicate an increase of the free volume of the PMPS polymer after introduction of ZIF-8 nanoparticles.

KW - Increased free volume

KW - Mixed matrix membrane

KW - Permeation

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