Enabling simultaneous CO2 and water vapor removal by MOF-801/Pebax mixed matrix membranes: Molecular simulation and experimental study

Dehydration and CO 2 removal are two important gas separation processes. An efficient membrane enabling simultaneous reduction of water vapor and CO 2 levels from humid gas streams, such as natural gas and power plant flue gas, may advance these processes. In this study, a water-harvesting metal-organic framework, MOF-801, was synthesized with an average particle size of 120 nm, which was then dispersed in a Pebax matrix to fabricate mixed matrix membranes (MMMs). The potential of the MOF-801 as a filler in MMMs was evaluated for water and CO 2 separation from CO 2 /N 2 and CO 2 /CH 4 mixed gas streams. Compared with the neat Pebax membrane, 70% enhancement in the water permeability was achieved for an MMM of 20 wt.% MOF loading at 10 bar with a humid feed composition of CO 2 /CH 4 . A considerable CO 2 /N 2 separation factor (108) and CO 2 permeability (270 Barrer) were also obtained, exceeding the Robeson upper bound at both dry and humid states. A molecular simulation study was performed to reveal the adsorption sites in the MOF lattice and favorable interactions with gases. Interestingly, competition between gas components close to the Zr atom was observed, which is the favorable site for both CO 2 and water. Competitive adsorption was found to be the dominating transport mechanism for the selective transport of CO 2 and H 2 O in MOF-801, revealing the role of MOF-801 in MMMs for CO 2 and water vapor separation under both humid and dry conditions.

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Publication Details

Journal
Carbon Capture Science & Technology
Published
2024-09-26
DOI
https://doi.org/10.1016/j.ccst.2024.100307
Citations
3
Primary Topic
Membrane Separation and Gas Transport
Type
article
Field-Weighted Citation Impact
0.64

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article

Enabling simultaneous CO2 and water vapor removal by MOF-801/Pebax mixed matrix membranes: Molecular simulation and experimental study

Saravanan Janakiram, Sadiye Velioğlu, Brian A. Grimes, Magne Hillestad et al.
3 citations
Carbon Capture Science & Technology
Membrane Separation and Gas Transport
0.64
article

Enabling simultaneous CO2 and water vapor removal by MOF-801/Pebax mixed matrix membranes: Molecular simulation and experimental study

Saravanan Janakiram, Sadiye Velioğlu, Brian A. Grimes, Magne Hillestad, Mahdi Ahmadi, Arne Lindbråthen, Liyuan Deng
article en
3 citations

Abstract

Dehydration and CO 2 removal are two important gas separation processes. An efficient membrane enabling simultaneous reduction of water vapor and CO 2 levels from humid gas streams, such as natural gas and power plant flue gas, may advance these processes. In this study, a water-harvesting metal-organic framework, MOF-801, was synthesized with an average particle size of 120 nm, which was then dispersed in a Pebax matrix to fabricate mixed matrix membranes (MMMs). The potential of the MOF-801 as a filler in MMMs was evaluated for water and CO 2 separation from CO 2 /N 2 and CO 2 /CH 4 mixed gas streams. Compared with the neat Pebax membrane, 70% enhancement in the water permeability was achieved for an MMM of 20 wt.% MOF loading at 10 bar with a humid feed composition of CO 2 /CH 4 . A considerable CO 2 /N 2 separation factor (108) and CO 2 permeability (270 Barrer) were also obtained, exceeding the Robeson upper bound at both dry and humid states. A molecular simulation study was performed to reveal the adsorption sites in the MOF lattice and favorable interactions with gases. Interestingly, competition between gas components close to the Zr atom was observed, which is the favorable site for both CO 2 and water. Competitive adsorption was found to be the dominating transport mechanism for the selective transport of CO 2 and H 2 O in MOF-801, revealing the role of MOF-801 in MMMs for CO 2 and water vapor separation under both humid and dry conditions.

Carbon Capture Science & TechnologyVol. 13
Gebze Technical University (TR), Norwegian University of Science and Technology (NO), Institute of Nanotechnology (GB)
Norges Forskningsråd
Clean water and sanitation
Openalex Percentile: Top 36%
Membrane Separation and Gas Transport
0.64
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