选择性
巴勒
膜
气体分离
材料科学
化学工程
分子筛
烟气
碳纤维
氟
渗透
有机化学
纳米技术
吸附
催化作用
化学
复合材料
生物化学
复合数
工程类
冶金
作者
Shan Xu,Guobao Li,Ruirui Yu,Pan Wang,Yunlong Ji
标识
DOI:10.1002/adma.202420477
摘要
Abstract Increasing energy consumption and climate change present an urgent global challenge to achieve carbon neutrality, with CO 2 capture as a top priority. Among various carbon capture technologies, CO 2 membrane separation stands out for its simplicity and energy efficiency in applications including gas purification and industrial gas recovery. Herein, a series of fluorine‐tailored porous carbon molecular sieve (CMS) membranes derived from precisely designed precursors, achieving a well‐balanced high permeability and selectivity for CO 2 separation are developed. Incorporating bent terphenyl monomers and both aliphatic/aromatic trifluoromethyl groups disrupted dense chain packing and promoted pore formation with enhanced permeability and selectivity for CO 2 separation. The TFM‐550 membrane, derived from a fluorinated stretched polymer backbone precursor, exhibits exceptional performance with a CO 2 permeability of 47 190 ± 3204 Barrer and a CO 2 /N 2 selectivity of 28.3 ± 5.7, while TFM‐800 presented a higher selectivity of 71.8 ± 11.5, surpassing the 2019 upper bound. Furthermore, under flue gas conditions (CO 2 /O 2 /N 2 = 1/1/4 in molar ratio), the CMS membrane demonstrate high CO 2 permeability of 36,204 ± 2,235 Barrer and outstanding CO 2 /N 2 selectivity of 35.3 ± 1.8. The results here highlight the effectiveness of fluorine tailoring and the potential of fluorinated CMS membranes for sustainable industrial carbon capture applications.
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