Computational fluid dynamics investigation of CO2 absorption using ionic liquids in hollow-fiber membrane contactors

This study integrates computational fluid dynamics (CFD) modeling with previously obtained experimental data to investigate the CO 2 absorption process using hollow fiber membrane contactors (HFMCs) and ionic liquids (ILs). Two types of HFMCs, polysulfone (PS) and polypropylene (PP), were tested in combination with two ILs: [emim][Ac] and [emim][EtSO 4 ]. The CFD models, developed using COMSOL Multiphysics, were validated against laboratory-scale experimental data. A strong correlation between the experimental and simulated results was observed, as indicated by high R 2 values (0.9208 to 0.9844) and low RMSE values (1.4657 to 2.1479), confirming the model's accuracy in representing the actual process. Among the ILs studied, [emim][Ac] showed superior CO 2 absorption efficiency due to its higher CO 2 solubility compared to [emim][EtSO 4 ]. Velocity and concentration profiles of both gas and liquid phases were determined, showcasing the ability of CFD modeling to predict key process parameters across the system geometry. Sensitivity analyses identified the optimal absorption temperature, membrane length, and gas velocity to achieve CO 2 absorption efficiency exceeding 90 %. Results showed that increasing the absorption temperature and membrane length significantly enhances the process performance. Additionally, incorporating shell baffles improved absorption efficiency by approximately 5 %, though it resulted in a notable increase in liquid pressure drop across the shell. • Computational fluid dynamics modeling and experimental analysis of nondispersive CO 2 absorption using hollow-fiber membrane contactors (HFMCs) • CO 2 absorption assessment using two ionic liquids, [emim][Ac] and [emim][EtSO 4 ], in polysulfone (PS) and polypropylene (PP) membrane contactors • Sensitivity analysis: variable membrane length and temperature to achieve over 90% absorption efficiency • Evaluation of different geometries by introducing vertical shell baffles to improve the absorption efficiency

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Publication Details

Journal
Chemical Engineering Journal
Published
2025-06-24
DOI
https://doi.org/10.1016/j.cej.2025.165308
Citations
5
Primary Topic
Carbon Dioxide Capture Technologies
Type
article
Field-Weighted Citation Impact
3.57
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article

Computational fluid dynamics investigation of CO2 absorption using ionic liquids in hollow-fiber membrane contactors

Alexandru-Constantin Bozonc, Ángel Irabien, Guillermo Díaz‐Sainz, Ana‐Maria Cormos
5 citations
Chemical Engineering Journal
Carbon Dioxide Capture Technologies
3.57
article

Computational fluid dynamics investigation of CO2 absorption using ionic liquids in hollow-fiber membrane contactors

Alexandru-Constantin Bozonc, Ángel Irabien, Guillermo Díaz‐Sainz, Ana‐Maria Cormos
article en
5 citations

Abstract

This study integrates computational fluid dynamics (CFD) modeling with previously obtained experimental data to investigate the CO 2 absorption process using hollow fiber membrane contactors (HFMCs) and ionic liquids (ILs). Two types of HFMCs, polysulfone (PS) and polypropylene (PP), were tested in combination with two ILs: [emim][Ac] and [emim][EtSO 4 ]. The CFD models, developed using COMSOL Multiphysics, were validated against laboratory-scale experimental data. A strong correlation between the experimental and simulated results was observed, as indicated by high R 2 values (0.9208 to 0.9844) and low RMSE values (1.4657 to 2.1479), confirming the model's accuracy in representing the actual process. Among the ILs studied, [emim][Ac] showed superior CO 2 absorption efficiency due to its higher CO 2 solubility compared to [emim][EtSO 4 ]. Velocity and concentration profiles of both gas and liquid phases were determined, showcasing the ability of CFD modeling to predict key process parameters across the system geometry. Sensitivity analyses identified the optimal absorption temperature, membrane length, and gas velocity to achieve CO 2 absorption efficiency exceeding 90 %. Results showed that increasing the absorption temperature and membrane length significantly enhances the process performance. Additionally, incorporating shell baffles improved absorption efficiency by approximately 5 %, though it resulted in a notable increase in liquid pressure drop across the shell. • Computational fluid dynamics modeling and experimental analysis of nondispersive CO 2 absorption using hollow-fiber membrane contactors (HFMCs) • CO 2 absorption assessment using two ionic liquids, [emim][Ac] and [emim][EtSO 4 ], in polysulfone (PS) and polypropylene (PP) membrane contactors • Sensitivity analysis: variable membrane length and temperature to achieve over 90% absorption efficiency • Evaluation of different geometries by introducing vertical shell baffles to improve the absorption efficiency

Chemical Engineering JournalVol. 519
Universidad de Cantabria (ES), Babeș-Bolyai University (RO)
Affordable and clean energy
Openalex Percentile: Top 7%
Carbon Dioxide Capture Technologies
3.57
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