4.8 Article

Ultra-selective molecular-sieving gas separation membranes enabled by multi-covalent-crosslinking of microporous polymer blends

Journal

NATURE COMMUNICATIONS
Volume 12, Issue 1, Pages -

Publisher

NATURE PORTFOLIO
DOI: 10.1038/s41467-021-26379-5

Keywords

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Funding

  1. National Natural Science Foundation of China [U1510123, 21603068, 21978321]
  2. Hundred Talents Program of Shanxi Province
  3. State Key Laboratory of Separation Membranes and Membrane Processes (Tiangong University) [M2-201801]
  4. Fundamental Research Funds for the Central Universities [DUT20RC(3)023]
  5. LiaoNing Revitalization Talents Program [XLYC2007008]

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Researchers have designed a porous polymer membrane with high permeability and selectivity through multi-crosslinking, surpassing traditional separation membrane limits. Adjusting reaction conditions can achieve ultra-selective gas separation.
Microporous polymers become increasingly attractive as materials for the fabrication of permeable and selective gas separation membranes but separation performance is often limited by broad pore size distribution. Here, the authors design a porous polymer membrane via multi-crosslinking of miscible blends of microporous polymers enabling simultaneous high permeability and selectivity. High-performance membranes exceeding the conventional permeability-selectivity upper bound are attractive for advanced gas separations. In the context microporous polymers have gained increasing attention owing to their exceptional permeability, which, however, demonstrate a moderate selectivity unfavorable for separating similarly sized gas mixtures. Here we report an approach to designing polymeric molecular sieve membranes via multi-covalent-crosslinking of blended bromomethyl polymer of intrinsic microporosity and Troger's base, enabling simultaneously high permeability and selectivity. Ultra-selective gas separation is achieved via adjusting reaction temperature, reaction time and the oxygen concentration with occurrences of polymer chain scission, rearrangement and thermal oxidative crosslinking reaction. Upon a thermal treatment at 300 degrees C for 5 h, membranes exhibit an O-2/N-2, CO2/CH4 and H-2/CH4 selectivity as high as 11.1, 154.5 and 813.6, respectively, transcending the state-of-art upper bounds. The design strategy represents a generalizable approach to creating molecular-sieving polymer membranes with enormous potentials for high-performance separation processes.

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