巴勒
选择性
膜
气体分离
吸附
磁导率
热扩散率
化学工程
材料科学
纳米技术
渗透
动能
化学
航程(航空)
膜技术
工艺工程
分离(统计)
选择性吸附
计算机科学
大规模运输
合成膜
膜透性
作者
Yawei Gu,Rujing Hou,Yizhen Situ,Bo Shen,Jingxian Hua,Zemin Li,Haiqian Lian,Chenkai Gu,QingYuan YANG,M. P. HILL,Weihong Xing,Yichang Pan
标识
DOI:10.1002/anie.202521250
摘要
Metal-organic frameworks (MOFs) offer exceptional tunability in pore structure and functionality, holding considerable potential for advanced gas separation membranes. However, their advancement is restricted by the permeability-selectivity trade-off and inefficient empirical screening. Herein, we propose an adsorption-diffusion dual-driven design strategy balancing moderate CO2 adsorption affinity (1 < αads,HTCS < 10) and high CO2 diffusivity selectivity (αdiff,HTCS > 10) within a pore-limiting diameter range of 3.8-4.4 Å. This rationale is corroborated by high-throughput computational screening and experimental membrane performance. Three yfm-topology MOF membranes-CAU-10H, CAU-10pydc, and KMF-1 with finely tuned pore microenvironments were synthesized, with the former two meeting the proposed criteria and KMF-1 serving as a counterexample. As anticipated, CAU-10H and CAU-10pydc exceed the 2019 upper bound for CO2/CH4 separation, with CAU-10pydc exhibiting a remarkable CO2 permeability of ∼2847 Barrer and a selectivity of 185, outperforming most state-of-the-art membranes. Moreover, despite sharing the same kinetic diameter as CO2, C2H2 exhibits 1.5 times higher adsorption affinity, resulting in a significantly lower permeability of only 39 Barrer under the same conditions. These results confirm the adsorption-diffusion dual-driven design principle, providing both theoretical insight and practical guidance for other challenging gas separation scenarios.
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