Membranes with ultrahigh permeance and practical selectivity could greatly decrease the cost of difficult industrial gas separations, such as CH/N separation. Advanced membranes made from porous materials, such as metal-organic frameworks, can achieve a good gas separation performance, although they are typically formed on support layers or mixed with polymeric matrices, placing limitations on gas permeance. Here an amorphous glass foam, aZIF-62, wherein a, g and f denote amorphous, glass and foam, respectively, was synthesized by a polymer-thermal-decomposition-assisted melting strategy, starting from a crystalline zeolitic imidazolate framework, ZIF-62. The thermal decomposition of incorporated low-molecular-weight polyethyleneimine evolves CO, NH and HO gases, creating a large number and variety of pores. This greatly increases pore interconnectivity but maintains the crystalline ZIF-62 ultramicropores, allowing ultrahigh gas permeance and good selectivity. A self-supported circular aZIF-62 with a thickness of 200-330 µm and area of 8.55 cm was used for membrane separation. The membranes perform well, showing a CH permeance of 30,000-50,000 gas permeance units, approximately two orders of magnitude higher than that of other reported membranes, with good CH/N selectivity (4-6).
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http://dx.doi.org/10.1038/s41563-023-01545-w | DOI Listing |
J Colloid Interface Sci
January 2025
Jilin Provincial Science and Technology Innovation Centre of Optical Materials and Chemistry, School of Chemistry and Environmental Engineering, Changchun University of Science and Technology, Changchun 130022, China. Electronic address:
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UMR CNRS 5629, laboratoire LCPO, Université de Bordeaux, Pessac, F-33600, France.
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Lam Research, Tualatin, Oregon 97062, USA.
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