Silica/Polyimide Mixed Matrix Membrane for <scp>CO<sub>2</sub></scp>/<scp>CH<sub>4</sub></scp> and <scp>O<sub>2</sub></scp>/<scp>N<sub>2</sub></scp> Gas Separation: A Computational Approach

ABSTRACT Silica‐incorporated polyimide (PI)‐based mixed matrix membranes (MMMs) are emerging as promising candidates for gas separation. However, experimental evaluation of their performance is challenging due to the complex interactions between polymers and fillers and limitations in isolating individual transport mechanisms. This study employs Monte Carlo and molecular dynamics (MD) simulations to investigate the solubility and diffusivity of CO 2 /CH 4 and O 2 /N 2 in silica/6FDA‐ODA PI MMMs with varying silica loadings (0–20 wt%). The mixed gas compositions are chosen to reflect real‐world conditions, as 30% CO 2 in CO 2 /CH 4 mixtures, representative of sour gas in natural reserves, and 21% O 2 in O 2 /N 2 mixtures, mimicking air composition. Results indicate that incorporating 10 wt% silica enhances CO 2 permeability by 270% and CO 2 /CH 4 selectivity by 136% compared to pristine 6FDA‐ODA PI. For O 2 /N 2 separation, an O 2 permeability of 23.59 and selectivity of 3.11 were achieved. These findings align well with the experimental literature, with 0.01%–10.4% deviation. Benchmarking confirms superior permeability over reported membranes, highlighting the potential of silica/6FDA‐ODA PI MMMs for efficient gas separation. This study provides valuable molecular‐level insights, paving the way for the rational design of high‐performance membranes for industrial applications.

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Publication Details

Journal
Journal of Applied Polymer Science
Published
2025-05-29
DOI
https://doi.org/10.1002/app.57335
Primary Topic
Membrane Separation and Gas Transport
Type
article
Field-Weighted Citation Impact
0.00

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article

Silica/Polyimide Mixed Matrix Membrane for CO2/CH4 and O2/N2 Gas Separation: A Computational Approach

Irene Sow Mei Lock, Bridgid Lai Fui Chin, Chung Loong Yiin, Lam Ghai Lim et al.
Journal of Applied Polymer Science
Membrane Separation and Gas Transport
article

Silica/Polyimide Mixed Matrix Membrane for CO2/CH4 and O2/N2 Gas Separation: A Computational Approach

Irene Sow Mei Lock, Bridgid Lai Fui Chin, Chung Loong Yiin, Lam Ghai Lim, Serene Sow Mun Lock, Suhaib Umer Ilyas, Mehtab Ali Darban, Xiau Jia Liew
article en

Abstract

ABSTRACT Silica‐incorporated polyimide (PI)‐based mixed matrix membranes (MMMs) are emerging as promising candidates for gas separation. However, experimental evaluation of their performance is challenging due to the complex interactions between polymers and fillers and limitations in isolating individual transport mechanisms. This study employs Monte Carlo and molecular dynamics (MD) simulations to investigate the solubility and diffusivity of CO 2 /CH 4 and O 2 /N 2 in silica/6FDA‐ODA PI MMMs with varying silica loadings (0–20 wt%). The mixed gas compositions are chosen to reflect real‐world conditions, as 30% CO 2 in CO 2 /CH 4 mixtures, representative of sour gas in natural reserves, and 21% O 2 in O 2 /N 2 mixtures, mimicking air composition. Results indicate that incorporating 10 wt% silica enhances CO 2 permeability by 270% and CO 2 /CH 4 selectivity by 136% compared to pristine 6FDA‐ODA PI. For O 2 /N 2 separation, an O 2 permeability of 23.59 and selectivity of 3.11 were achieved. These findings align well with the experimental literature, with 0.01%–10.4% deviation. Benchmarking confirms superior permeability over reported membranes, highlighting the potential of silica/6FDA‐ODA PI MMMs for efficient gas separation. This study provides valuable molecular‐level insights, paving the way for the rational design of high‐performance membranes for industrial applications.

Journal of Applied Polymer ScienceVol. 142(34)
Monash University Malaysia (MY), Curtin University Sarawak (MY), Petronas (Malaysia) (MY), Universiti Teknologi Petronas (MY), Universiti Malaysia Sarawak (MY), University of Jeddah (SA)
Ministry of Higher Education, Yayasan UTP
Industry, innovation and infrastructure
Openalex Percentile: Top 89%
Membrane Separation and Gas Transport
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