Mass transport limitations in high-performance water-vapor selective membranes: A multiphysics simulation approach

• Cell geometry and flow reduce membrane performance by ∼20% compared to intrinsic values. • Boundary layer growth impacts membrane performance evaluation. • Test cells show hotspots and dead zones, limiting active membrane area performance. • Scaling membrane lengths from 1 mm to 40 mm reduces performance by 10–50%. The pursuit of high-performance, water–vapor selective membranes remain a focal point, as membranes often emerge as energy-efficient alternatives for psychrometric processes. Recent literature results on membranes fabricated from specialized polymers, 2D materials, and metal–organic frameworks (MOFs) as selective layers, have demonstrated unprecedented water vapour permeance and selectivity. However, few studies have examined how such high intrinsic permeances interplay with transport limitations governing the overall membrane performance in common test-cell geometries. This study aims to assess the theoretical limits of diffusion-based membranes by studying the impact of various transport resistances on the overall system permeance. Multiphysics simulations are used to model both fluid dynamics and mass transport within a simplistic geometry versus a commercially available sweep cell. A non-uniform flux pattern emerges, highlighting the substantial impact of non-uniform flow fields and fluid boundary layers, which were previously deemed inconsequential in gas separations. This leads to the underutilization of the membrane, yet unexpectedly increases the overall process permeance by approximately 20% when compared to a simple planar geometry. As researchers engineer better selective layers, future advancements could push this difference as high as 36%. By utilizing dimensionless groups and fitting parameters (0.76 Re 0.438 Sc 0.33 ), the true membrane permeance can be extracted from the test configuration within a 5% margin of error. This approach is essential for assessing permeances, scaling membranes, and enabling accurate comparisons.

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Publication Details

Journal
Chemical Engineering Journal
Published
2025-02-24
DOI
https://doi.org/10.1016/j.cej.2025.160974
Citations
1
Primary Topic
Membrane Separation Technologies
Type
article
Field-Weighted Citation Impact
0.82

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article

Mass transport limitations in high-performance water-vapor selective membranes: A multiphysics simulation approach

Saeed Ghanbari, Jeff T. Gostick, Ahmed A. Abdala, Mahshid Chekini et al.
1 citations
Chemical Engineering Journal
Membrane Separation Technologies
0.82
article

Mass transport limitations in high-performance water-vapor selective membranes: A multiphysics simulation approach

Saeed Ghanbari, Jeff T. Gostick, Ahmed A. Abdala, Mahshid Chekini, Kiyoumars Zarshenas, Nathan Grishkewich, Michael A. Pope, Nikolai D. Burton
article en
1 citations

Abstract

• Cell geometry and flow reduce membrane performance by ∼20% compared to intrinsic values. • Boundary layer growth impacts membrane performance evaluation. • Test cells show hotspots and dead zones, limiting active membrane area performance. • Scaling membrane lengths from 1 mm to 40 mm reduces performance by 10–50%. The pursuit of high-performance, water–vapor selective membranes remain a focal point, as membranes often emerge as energy-efficient alternatives for psychrometric processes. Recent literature results on membranes fabricated from specialized polymers, 2D materials, and metal–organic frameworks (MOFs) as selective layers, have demonstrated unprecedented water vapour permeance and selectivity. However, few studies have examined how such high intrinsic permeances interplay with transport limitations governing the overall membrane performance in common test-cell geometries. This study aims to assess the theoretical limits of diffusion-based membranes by studying the impact of various transport resistances on the overall system permeance. Multiphysics simulations are used to model both fluid dynamics and mass transport within a simplistic geometry versus a commercially available sweep cell. A non-uniform flux pattern emerges, highlighting the substantial impact of non-uniform flow fields and fluid boundary layers, which were previously deemed inconsequential in gas separations. This leads to the underutilization of the membrane, yet unexpectedly increases the overall process permeance by approximately 20% when compared to a simple planar geometry. As researchers engineer better selective layers, future advancements could push this difference as high as 36%. By utilizing dimensionless groups and fitting parameters (0.76 Re 0.438 Sc 0.33 ), the true membrane permeance can be extracted from the test configuration within a 5% margin of error. This approach is essential for assessing permeances, scaling membranes, and enabling accurate comparisons.

Chemical Engineering JournalVol. 508
University of Waterloo (CA), St Joseph's Health Centre (CA), Hamad bin Khalifa University (QA)
Mitacs, Qatar National Research Fund, Natural Sciences and Engineering Research Council of Canada
Clean water and sanitation
Openalex Percentile: Top 29%
Membrane Separation Technologies
0.82
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