Long-term pure- and mixed-gas performance of carbon molecular sieve membranes derived from a tetraphenylethylene-based ladder polymer of intrinsic microporosity (TPE-PIM) for propylene/propane separation

Continuous long-term evaluation of propylene and propane permeation through narrow slit carbon molecular sieve (CMS) membranes is essential for an in-depth study of their steady-state separation performance. CMS membranes are characterized by finely tuned ultramicroporous structures, exceptional thermal and chemical stability, and hold great promise for the energy-intensive separation of propylene and propane. However, the gradual changes in their performance over time due to penetrant-induced structural chain rearrangements have often been overlooked. In this study, we prepared CMS membranes using a polymer of intrinsic microporosity (PIM) with a highly aromatic tetraphenylethylene (TPE) based building block. The presence of bulky and sterically hindered TPE repeat units renders this polymer an excellent precursor for the fabrication of high-performance CMS membranes. The TPE-PIM-based precursor underwent pyrolysis at temperatures ranging from 550 to 700 °C for 1 h. Pure- and mixed-gas permeation tests were accompanied by various characterization techniques to assess the carbonization state of the CMS materials. The CMS pyrolyzed at 700 °C exhibited a decline in pure-gas C 3 H 6 /C 3 H 8 selectivity from an initial value of 300 to 161 at steady state over a 20-day period. Even more notable, under equimolar mixed-gas feed conditions, the isotropic CMS film displayed a substantial C 3 H 6 /C 3 H 8 selectivity reduction from 214 to 62 over a 24-day period. This performance decline can be attributed to competitive sorption and very slow dilation kinetics, which led to moderately reduced propylene permeability while significantly enhancing propane permeability. Our study suggests that long-term, continuously performed mixed-gas permeation experiments are essential to assess the ‘steady-state’ performance of CMS membranes for mixtures containing highly sorbing feed components, as observed for propylene/propane separation. • TPE-PIM-derived CMS films require very long time to reach steady-state permeability for C 3 H 8 . • Propane sorption at 1 bar in TPE-PIM-based CMS pyrolized at 600–700 °C requires ∼ 3–4 days to reach equilibrium. • Continuous long-term mixed-gas permeability experiments are essential to obtain reliable performance data for C 3 H 6 /C 3 H 8 . • Steady-state mixed-gas C 3 H 6 permeability of 7.5 Barrer and C 3 H 6 /C 3 H 8 selectivity of 62 for TPE-PIM-700 °C after 24 days.

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Publication Details

Journal
Journal of Membrane Science
Published
2024-08-29
DOI
https://doi.org/10.1016/j.memsci.2024.123255
Citations
9
Primary Topic
Membrane Separation and Gas Transport
Type
article
Field-Weighted Citation Impact
1.91

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article

Long-term pure- and mixed-gas performance of carbon molecular sieve membranes derived from a tetraphenylethylene-based ladder polymer of intrinsic microporosity (TPE-PIM) for propylene/propane separation

Nimer Wehbe, Fawwaz Elahi, Khalid Hazazi, Ingo Pinnau et al.
9 citations
Journal of Membrane Science
Membrane Separation and Gas Transport
1.91
article

Long-term pure- and mixed-gas performance of carbon molecular sieve membranes derived from a tetraphenylethylene-based ladder polymer of intrinsic microporosity (TPE-PIM) for propylene/propane separation

Nimer Wehbe, Fawwaz Elahi, Khalid Hazazi, Ingo Pinnau, Yingge Wang, Marcel Balçık, Feng Xu, Vikas Kumar
article en
9 citations

Abstract

Continuous long-term evaluation of propylene and propane permeation through narrow slit carbon molecular sieve (CMS) membranes is essential for an in-depth study of their steady-state separation performance. CMS membranes are characterized by finely tuned ultramicroporous structures, exceptional thermal and chemical stability, and hold great promise for the energy-intensive separation of propylene and propane. However, the gradual changes in their performance over time due to penetrant-induced structural chain rearrangements have often been overlooked. In this study, we prepared CMS membranes using a polymer of intrinsic microporosity (PIM) with a highly aromatic tetraphenylethylene (TPE) based building block. The presence of bulky and sterically hindered TPE repeat units renders this polymer an excellent precursor for the fabrication of high-performance CMS membranes. The TPE-PIM-based precursor underwent pyrolysis at temperatures ranging from 550 to 700 °C for 1 h. Pure- and mixed-gas permeation tests were accompanied by various characterization techniques to assess the carbonization state of the CMS materials. The CMS pyrolyzed at 700 °C exhibited a decline in pure-gas C 3 H 6 /C 3 H 8 selectivity from an initial value of 300 to 161 at steady state over a 20-day period. Even more notable, under equimolar mixed-gas feed conditions, the isotropic CMS film displayed a substantial C 3 H 6 /C 3 H 8 selectivity reduction from 214 to 62 over a 24-day period. This performance decline can be attributed to competitive sorption and very slow dilation kinetics, which led to moderately reduced propylene permeability while significantly enhancing propane permeability. Our study suggests that long-term, continuously performed mixed-gas permeation experiments are essential to assess the ‘steady-state’ performance of CMS membranes for mixtures containing highly sorbing feed components, as observed for propylene/propane separation. • TPE-PIM-derived CMS films require very long time to reach steady-state permeability for C 3 H 8 . • Propane sorption at 1 bar in TPE-PIM-based CMS pyrolized at 600–700 °C requires ∼ 3–4 days to reach equilibrium. • Continuous long-term mixed-gas permeability experiments are essential to obtain reliable performance data for C 3 H 6 /C 3 H 8 . • Steady-state mixed-gas C 3 H 6 permeability of 7.5 Barrer and C 3 H 6 /C 3 H 8 selectivity of 62 for TPE-PIM-700 °C after 24 days.

Journal of Membrane ScienceVol. 713
King Abdullah University of Science and Technology (SA)
King Abdullah University of Science and Technology
Openalex Percentile: Top 15%
Membrane Separation and Gas Transport
1.91
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