Turning Microstructure in Block Copolymer Membranes: A Facile Strategy to Improve CO <sub>2</sub> Separation Performance

To mitigate global climate change, the development of membranes with high CO<sub>2</sub> permeability and selectivity is urgently needed. Here, a simple and effective non-solvent-induced microstructure rearrangement (MSR) technique is proposed to enhance the gas separation performance of Pebax 2533 membranes. By immersing Pebax 2533 membranes in amino acid salt solutions to induce MSR, the CO<sub>2</sub> permeability of the optimized Pebax 2533-GlyK 10 wt.% membrane reached 1180 Barrer, a 4.5-fold increase compared to the original membrane, without compromising CO<sub>2</sub>/N<sub>2</sub> selectivity. Moreover, the MSR membrane maintains stable gas separation performance for nearly 500 days, demonstrating excellent long-term stability. Furthermore, applying the MSR technique to thin-film composite (TFC) membranes revealed that both Pebax 2533/polyvinyl chloride (PVC) hollow fiber (HF) TFC membranes and Pebax 2533/polyacrylonitrile (PAN) flat-sheet TFC membranes exhibited significantly enhanced CO<sub>2</sub> permeance under the treatment of DI water. Characterization results indicated that the chemical-physical properties of the membranes before and after MSR are nearly unchanged, suggesting that the non-solvent-induced MSR is a promising technique for next-generation membrane development for carbon capture.

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Publication Details

Journal
Advanced Science
Published
2025-04-17
DOI
https://doi.org/10.1002/advs.202501330
Citations
8
Primary Topic
Membrane Separation and Gas Transport
Type
article
Field-Weighted Citation Impact
5.71

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article

Turning Microstructure in Block Copolymer Membranes: A Facile Strategy to Improve CO 2 Separation Performance

Zikang Qin, Zhongde Dai, Roman Selyanchyn, Yuanfa Zhuang et al.
8 citations
Advanced Science
Membrane Separation and Gas Transport
5.71
article

Turning Microstructure in Block Copolymer Membranes: A Facile Strategy to Improve CO 2 Separation Performance

Zikang Qin, Zhongde Dai, Roman Selyanchyn, Yuanfa Zhuang, Hongyong Zhao, Liyuan Deng, Dengguo Yin, Bart Van der Bruggen, Wenju Jiang, Junfeng Zheng, Yujie Li, Lu Yao, Jie Dong, Min Deng, Lin Yang, Weiyi Zhao, Jing Wei
article en
8 citations

Abstract

To mitigate global climate change, the development of membranes with high CO<sub>2</sub> permeability and selectivity is urgently needed. Here, a simple and effective non-solvent-induced microstructure rearrangement (MSR) technique is proposed to enhance the gas separation performance of Pebax 2533 membranes. By immersing Pebax 2533 membranes in amino acid salt solutions to induce MSR, the CO<sub>2</sub> permeability of the optimized Pebax 2533-GlyK 10 wt.% membrane reached 1180 Barrer, a 4.5-fold increase compared to the original membrane, without compromising CO<sub>2</sub>/N<sub>2</sub> selectivity. Moreover, the MSR membrane maintains stable gas separation performance for nearly 500 days, demonstrating excellent long-term stability. Furthermore, applying the MSR technique to thin-film composite (TFC) membranes revealed that both Pebax 2533/polyvinyl chloride (PVC) hollow fiber (HF) TFC membranes and Pebax 2533/polyacrylonitrile (PAN) flat-sheet TFC membranes exhibited significantly enhanced CO<sub>2</sub> permeance under the treatment of DI water. Characterization results indicated that the chemical-physical properties of the membranes before and after MSR are nearly unchanged, suggesting that the non-solvent-induced MSR is a promising technique for next-generation membrane development for carbon capture.

Advanced ScienceVol. 12(25)
University of Science and Technology of China (CN), Kyushu University (JP), Tiangong University (CN), Norwegian University of Science and Technology (NO), Sichuan University (CN), Dongfang Electric Corporation (China) (CN), National Synchrotron Radiation Laboratory (CN), Imperial College London (GB), KU Leuven (BE)
National Natural Science Foundation of China, Japan Society for the Promotion of Science
Climate action
Openalex Percentile: Top 4%
Membrane Separation and Gas Transport
5.71
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