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

M Marta Pérez‐Miana (Nanoscience and Materials Institute of Aragon (INMA) CSIC‐Universidad de Zaragoza Mariano Esquillor St. Zaragoza 50018 Spain) J José Miguel Luque‐Alled (Nanoscience and Materials Institute of Aragon (INMA) CSIC‐Universidad de Zaragoza Mariano Esquillor St. Zaragoza 50018 Spain) A Alvaro Mayoral (Centre for High-Resolution Electron Microscopy (CℏEM), School of Physical Science and Technology and Shanghai Key Laboratory of High-Resolution Electron Microscopy) Íñigo Martínez‐Visus (Nanoscience and Materials Institute of Aragon (INMA) CSIC‐Universidad de Zaragoza Mariano Esquillor St. Zaragoza 50018 Spain) A Andrew B. Foster (Department of Chemistry School of Natural Sciences The University of Manchester Manchester M13 9PL UK) P Peter M. Budd (Department of Chemistry School of Natural Sciences The University of Manchester Manchester M13 9PL UK) J Joaquín Coronas (Nanoscience and Materials Institute of Aragon (INMA) CSIC‐Universidad de Zaragoza Mariano Esquillor St. Zaragoza 50018 Spain)

Abstract

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 2 , 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 2 adsorption capacity (2.34 mmol g −1 at 90 kPa and 0 °C). Gas separation experiments were performed using mixed gas compositions of 15/85 CO 2 /N 2 at 3 bar and 35 °C. The resulting MMM with a 5 wt.% loading exhibited an enhanced CO 2 separation performance, with ca. 70% and 10% increases in CO 2 permeability (8900 Barrer) and CO 2 /N 2 selectivity (20.2), respectively, compared to pristine PIM‐1 membranes. In addition, thin film nanocomposite membranes were prepared showing a 23.5 CO 2 /N 2 selectivity at 2350 GPU of CO 2 . This modification strategy shows a great potential for improving the CO 2 capture technologies, highlighting the potential of tailoring MOF fillers for advanced membrane materials in gas separation applications.

Article Details

Volume / Issue Vol. 64, Issue 22
Published May 26, 2025
ISSN 1433-7851
Publisher Wiley

Journal Info

Angewandte Chemie International Edition

Wiley

ISSN: 1433-7851 Physical Sciences

Authors (7)

M

Marta Pérez‐Miana

Nanoscience and Materials Institute of Aragon (INMA) CSIC‐Universidad de Zaragoza Mariano Esquillor St. Zaragoza 50018 Spain

J

José Miguel Luque‐Alled

Nanoscience and Materials Institute of Aragon (INMA) CSIC‐Universidad de Zaragoza Mariano Esquillor St. Zaragoza 50018 Spain

A

Alvaro Mayoral

Centre for High-Resolution Electron Microscopy (CℏEM), School of Physical Science and Technology and Shanghai Key Laboratory of High-Resolution Electron Microscopy

Íñigo Martínez‐Visus

Nanoscience and Materials Institute of Aragon (INMA) CSIC‐Universidad de Zaragoza Mariano Esquillor St. Zaragoza 50018 Spain

A

Andrew B. Foster

Department of Chemistry School of Natural Sciences The University of Manchester Manchester M13 9PL UK

P

Peter M. Budd

Department of Chemistry School of Natural Sciences The University of Manchester Manchester M13 9PL UK

J

Joaquín Coronas

Nanoscience and Materials Institute of Aragon (INMA) CSIC‐Universidad de Zaragoza Mariano Esquillor St. Zaragoza 50018 Spain