Restricting ionic liquid in a network comprising of GO/CNT as a separation membrane for efficient CO2 capture

The release of carbon dioxide (CO 2 ) to the atmosphere remains a critical challenge in addressing climate change, with emissions from power plants being a primary contributor. Membrane-based separation processes offer cost-effective, robust, and energy efficient alternatives to CO 2 capture from power plants. Ionic liquids (IL), known for their high CO 2 affinity, low vapor pressure, and high thermal stability, are propitious materials for such separations. In this study, we try to address major challenges currently restricting IL-based membranes including the porous structure for loading IL and the loading procedure onto the porous structure. An ultrathin (∼230 nm) 2–dimensional composite network comprising of graphene oxide (GO) sheets intercalated carbon nanotubes (CNT) spatially confining IL targeting high CO 2 permeance was designed and fabricated. An IL, 1-ethyl-3 methylimidazolium tetrafluoroborate ([EMIM][BF 4 ] was used as the active separating medium. This GO/CNT hybrid network not only stabilizes the IL within the nanochannels because of interactions between cations of IL and negatively charged functional groups on GO (carboxyl, hydroxyl and carboxy groups) but also facilitates faster transport (increased nanochannels because of CNT incorporation) yielding a CO 2 permeance of ∼600 GPU (one order of magnitude higher than reported membranes employing the same ionic liquid) and a CO 2 /N 2 selectivity of 62 under humid conditions and elevated temperatures (up to 80 ºC). Our approach provides a modified strategy of using ionic liquids in the solution form as opposed to most studies using pure form for obtaining a scalable, ultrathin, stable supported IL membrane.

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Publication Details

Journal
Advanced Membranes
Published
2025-01-01
DOI
https://doi.org/10.1016/j.advmem.2025.100158
Citations
2
Primary Topic
Membrane Separation and Gas Transport
Type
article
Field-Weighted Citation Impact
1.43

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article

Restricting ionic liquid in a network comprising of GO/CNT as a separation membrane for efficient CO2 capture

Qiaobei Dong, Miao Yu, Dinesh Behera, Bratin Sengupta et al.
2 citations
Advanced Membranes
Membrane Separation and Gas Transport
1.43
article

Restricting ionic liquid in a network comprising of GO/CNT as a separation membrane for efficient CO2 capture

Qiaobei Dong, Miao Yu, Dinesh Behera, Bratin Sengupta, Shiguang Li, Weiwei Xu, Fan Wang
article en
2 citations

Abstract

The release of carbon dioxide (CO 2 ) to the atmosphere remains a critical challenge in addressing climate change, with emissions from power plants being a primary contributor. Membrane-based separation processes offer cost-effective, robust, and energy efficient alternatives to CO 2 capture from power plants. Ionic liquids (IL), known for their high CO 2 affinity, low vapor pressure, and high thermal stability, are propitious materials for such separations. In this study, we try to address major challenges currently restricting IL-based membranes including the porous structure for loading IL and the loading procedure onto the porous structure. An ultrathin (∼230 nm) 2–dimensional composite network comprising of graphene oxide (GO) sheets intercalated carbon nanotubes (CNT) spatially confining IL targeting high CO 2 permeance was designed and fabricated. An IL, 1-ethyl-3 methylimidazolium tetrafluoroborate ([EMIM][BF 4 ] was used as the active separating medium. This GO/CNT hybrid network not only stabilizes the IL within the nanochannels because of interactions between cations of IL and negatively charged functional groups on GO (carboxyl, hydroxyl and carboxy groups) but also facilitates faster transport (increased nanochannels because of CNT incorporation) yielding a CO 2 permeance of ∼600 GPU (one order of magnitude higher than reported membranes employing the same ionic liquid) and a CO 2 /N 2 selectivity of 62 under humid conditions and elevated temperatures (up to 80 ºC). Our approach provides a modified strategy of using ionic liquids in the solution form as opposed to most studies using pure form for obtaining a scalable, ultrathin, stable supported IL membrane.

Advanced MembranesVol. 5
Gas Technology Institute (US), University at Buffalo, State University of New York (US)
U.S. Department of Energy
Affordable and clean energy
Openalex Percentile: Top 19%
Membrane Separation and Gas Transport
1.43
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