Amphiphilic Zeolitic Imidazolate Framework for Improved CO <sub>2</sub> Separation in PIM‐1 Mixed Matrix Membranes

This study aims to enhance the compatibility between filler and polymer in mixed matrix membranes (MMMs), addressing an important challenge in membrane development. ZIF-94, known for its affinity to CO<sub>2</sub>, was partially modified with 2-undecylimidazolate (umIm) through the solvent-assisted ligand exchange (SALE) method to improve its compatibility with the prototypical polymer of intrinsic microporosity PIM-1. The modified ZIF-94 (ZIF-94-umIm) can be considered as an amphiphilic MOF with both hydrophilic and hydrophobic moieties, while maintaining a considerably high CO<sub>2</sub> adsorption capacity (2.34 mmol g<sup>-1</sup> at 90 kPa and 0 °C). Gas separation experiments were performed using mixed gas compositions of 15/85 CO<sub>2</sub>/N<sub>2</sub> at 3 bar and 35 °C. The resulting MMM with a 5 wt.% loading exhibited an enhanced CO<sub>2</sub> separation performance, with ca. 70% and 10% increases in CO<sub>2</sub> permeability (8900 Barrer) and CO<sub>2</sub>/N<sub>2</sub> selectivity (20.2), respectively, compared to pristine PIM-1 membranes. In addition, thin film nanocomposite membranes were prepared showing a 23.5 CO<sub>2</sub>/N<sub>2</sub> selectivity at 2350 GPU of CO<sub>2</sub>. This modification strategy shows a great potential for improving the CO<sub>2</sub> capture technologies, highlighting the potential of tailoring MOF fillers for advanced membrane materials in gas separation applications.

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Publication Details

Journal
Angewandte Chemie International Edition
Published
2025-03-27
DOI
https://doi.org/10.1002/anie.202420879
Citations
13
Primary Topic
Membrane Separation and Gas Transport
Type
article
Field-Weighted Citation Impact
9.27

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article

Amphiphilic Zeolitic Imidazolate Framework for Improved CO 2 Separation in PIM‐1 Mixed Matrix Membranes

Íñigo Martínez‐Visus, Andrew B. Foster, José Miguel Luque‐Alled, Peter M. Budd et al.
13 citations
Angewandte Chemie International Edition
Membrane Separation and Gas Transport
9.27
article

Amphiphilic Zeolitic Imidazolate Framework for Improved CO 2 Separation in PIM‐1 Mixed Matrix Membranes

Íñigo Martínez‐Visus, Andrew B. Foster, José Miguel Luque‐Alled, Peter M. Budd, Marta Pérez-Miana, Álvaro Mayoral, Joaquı́n Coronas
article en
13 citations

Abstract

This study aims to enhance the compatibility between filler and polymer in mixed matrix membranes (MMMs), addressing an important challenge in membrane development. ZIF-94, known for its affinity to CO<sub>2</sub>, was partially modified with 2-undecylimidazolate (umIm) through the solvent-assisted ligand exchange (SALE) method to improve its compatibility with the prototypical polymer of intrinsic microporosity PIM-1. The modified ZIF-94 (ZIF-94-umIm) can be considered as an amphiphilic MOF with both hydrophilic and hydrophobic moieties, while maintaining a considerably high CO<sub>2</sub> adsorption capacity (2.34 mmol g<sup>-1</sup> at 90 kPa and 0 °C). Gas separation experiments were performed using mixed gas compositions of 15/85 CO<sub>2</sub>/N<sub>2</sub> at 3 bar and 35 °C. The resulting MMM with a 5 wt.% loading exhibited an enhanced CO<sub>2</sub> separation performance, with ca. 70% and 10% increases in CO<sub>2</sub> permeability (8900 Barrer) and CO<sub>2</sub>/N<sub>2</sub> selectivity (20.2), respectively, compared to pristine PIM-1 membranes. In addition, thin film nanocomposite membranes were prepared showing a 23.5 CO<sub>2</sub>/N<sub>2</sub> selectivity at 2350 GPU of CO<sub>2</sub>. This modification strategy shows a great potential for improving the CO<sub>2</sub> capture technologies, highlighting the potential of tailoring MOF fillers for advanced membrane materials in gas separation applications.

Angewandte Chemie International EditionVol. 64(22)
Universidad de Zaragoza (ES), University of Manchester (GB), Universitas Islam Al-Azhar Mataram (ID), Instituto de Nanociencia y Materiales de Aragón (ES)
European Commission, Engineering and Physical Sciences Research Council, European Regional Development Fund, Agencia Estatal de Investigación
Openalex Percentile: Top 2%
Membrane Separation and Gas Transport
9.27
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