Polysulfone/Graphene Oxide Mixed Matrix Membranes for Improved CO2/CH4 Separation

This research focuses on developing and optimizing mixed matrix membranes (MMMs) by incorporating graphene oxide (GO) into a polysulfone (PSF) matrix to enhance the separation performance of CO<sub>2</sub> and CH<sub>4</sub>. The morphology and gas separation performance of the MMMs were systematically characterized. The incorporation of GO enhanced gas permeation and CO<sub>2</sub>/CH<sub>4</sub> selectivity, as evaluated using a gas permeation setup. Notably, the PSF/GO-0.3 wt.% membrane exhibited superior performance, achieving a CO<sub>2</sub> permeability of 21.63 Barrer, among the highest reported for PSF-based MMMs. Additionally, the membrane demonstrated a CO<sub>2</sub>/CH<sub>4</sub> selectivity of 14.32, highlighting its effectiveness in distinguishing between the two gases, which is essential for carbon capture and natural gas decontamination applications. The uniform distribution of GO within the polymer matrix contributed to the membrane's enhanced performance. Furthermore, the MMMs exhibited outstanding resistance to CO<sub>2</sub> plasticization, with the PSF/GO-0.3 wt.% membrane maintaining its performance at pressures up to 10 bar, a significant improvement over the pristine PSF membrane, which failed at 4 bar. The improved plasticization resistance is ascribed to the reinforcing effect of GO, which stabilizes the polymer matrix, minimizing CO<sub>2</sub>-induced swelling. The PSF/GO-0.3 wt.% membrane exhibited exceptional CO<sub>2</sub> permeability, selectivity, and plasticization resistance, making it a viable alternative for industrial gas separation applications and outperforming previously reported PSF-based MMMs.

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Publication Details

Journal
Membranes
Published
2025-12-18
DOI
https://doi.org/10.3390/membranes15120386
Primary Topic
Membrane Separation and Gas Transport
Type
article
Field-Weighted Citation Impact
0.00

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article

Polysulfone/Graphene Oxide Mixed Matrix Membranes for Improved CO2/CH4 Separation

Membranes
Membrane Separation and Gas Transport
article

Polysulfone/Graphene Oxide Mixed Matrix Membranes for Improved CO2/CH4 Separation

article en

Abstract

This research focuses on developing and optimizing mixed matrix membranes (MMMs) by incorporating graphene oxide (GO) into a polysulfone (PSF) matrix to enhance the separation performance of CO<sub>2</sub> and CH<sub>4</sub>. The morphology and gas separation performance of the MMMs were systematically characterized. The incorporation of GO enhanced gas permeation and CO<sub>2</sub>/CH<sub>4</sub> selectivity, as evaluated using a gas permeation setup. Notably, the PSF/GO-0.3 wt.% membrane exhibited superior performance, achieving a CO<sub>2</sub> permeability of 21.63 Barrer, among the highest reported for PSF-based MMMs. Additionally, the membrane demonstrated a CO<sub>2</sub>/CH<sub>4</sub> selectivity of 14.32, highlighting its effectiveness in distinguishing between the two gases, which is essential for carbon capture and natural gas decontamination applications. The uniform distribution of GO within the polymer matrix contributed to the membrane's enhanced performance. Furthermore, the MMMs exhibited outstanding resistance to CO<sub>2</sub> plasticization, with the PSF/GO-0.3 wt.% membrane maintaining its performance at pressures up to 10 bar, a significant improvement over the pristine PSF membrane, which failed at 4 bar. The improved plasticization resistance is ascribed to the reinforcing effect of GO, which stabilizes the polymer matrix, minimizing CO<sub>2</sub>-induced swelling. The PSF/GO-0.3 wt.% membrane exhibited exceptional CO<sub>2</sub> permeability, selectivity, and plasticization resistance, making it a viable alternative for industrial gas separation applications and outperforming previously reported PSF-based MMMs.

MembranesVol. 15(12)
King Fahd University of Petroleum and Minerals (SA), University of Nottingham (GB), University of Jeddah (SA)
University of Jeddah
Industry, innovation and infrastructure
Openalex Percentile: Top 46%
Membrane Separation and Gas Transport
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