4.7 Article

Benchmark CO2 separation achieved by highly fluorinated nanoporous molecular sieve membranes from nonporous precursor via in situ cross-linking

期刊

JOURNAL OF MEMBRANE SCIENCE
卷 638, 期 -, 页码 -

出版社

ELSEVIER
DOI: 10.1016/j.memsci.2021.119698

关键词

Molecular sieve membrane; Cross-linking; Ultramicropore; Fluorine; CO2 separation

资金

  1. Division of Chemical Sciences, Geosciences, and Biosciences, Office of Basic Energy Sciences, US Department of Energy
  2. Department of Energy-Basic Energy Sciences [DE-AC02-07CH11358]

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This study successfully developed an in situ cross-linking strategy to prepare molecular sieve membranes with fluorinated micropores using polystyrene as a precursor template, which exhibit excellent performance in CO2/N-2 separation.
Molecular sieve membranes with rigid micropores and CO2-philic functionalities within the architectures are promising candidates in CO2 separation. However, the development of effective approaches for their fabrication still remains a significant challenge. Herein, an in situ cross-linking strategy is developed for the preparation of nanoporous fluorinated molecular sieve membranes using commercially available dense and non-porous polystyrene (MPS) as a precursor template. Based on the dehydrative Friedel-Crafts reactions with highly fluorinated benzylic alcohols, MPS membranes are cross-linked in situ upon exposure to Bronsted acid (CF3SO3H), affording fluorinated microporous polymeric membranes with surface areas up to 523 m(2) g(-1) and the presence of micropores centered at 1.1-1.3 nm as well as ultra-micropores (-0.6 nm). The obtained modified membranes exhibit good ideal CO2 permeability of 797 barrer and CO2/N-2 selectivity of 28.5. In addition, high fluorine content (up to 28.5 wt%) and good thermal stability made the cross-linked membranes promising candidates to produce fluorinated carbon molecular sieve membranes with improved textural properties, exhibiting surface areas up to 1020 m(2) g(-1) and ultra-micropores of -0.4 nm. These membranes achieve superior CO2/N-2 separation performances exceeding the Robeson upper bound limit (2008).

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