Carbon molecular sieve membrane with tunable microstructure for CO2 separation: Effect of multiscale structures of polyimide precursors

聚酰亚胺 渗透 微观结构 气体分离 材料科学 化学工程 聚合物 高分子化学 分子筛 部分 巴勒 二胺 化学 复合材料 有机化学 图层(电子) 吸附 生物化学 工程类
作者
Mengjie Hou,Wenbo Qi,Lin Li,Ruisong Xu,Jiajia Xue,Yongyue Zhang,Chengwen Song,Tonghua Wang
出处
期刊:Journal of Membrane Science [Elsevier]
卷期号:635: 119541-119541 被引量:98
标识
DOI:10.1016/j.memsci.2021.119541
摘要

Carbon molecular sieve (CMS) membranes were fabricated by designing the polyimides with different diamine moiety such as PPD, ODA, BAPP and BDAF to investigate the effects of multiscale structures of precursors on the microstructure and CO2 separation performance of the derived CMS membranes. The multiscale structures of polymeric precursor were characterized and simulated in terms of the characteristic of functional groups, the flatness of repeat units, the conformation of single chains, the packing efficiency of multi-chain network and the fractional free volume (FFV) of bulk polymers. The microstructure and CO2 separation performance of derived CMS membrane were characterized by XRD, TEM and gas permeation measurements. The CO2 permeation behavior of CMS membranes derived from different precursors was analyzed. Results indicated that the multiscale structures of polyimides significantly influenced the microstructure and CO2 separation performance of derived CMS membranes. Increased FFV (or reduced flatness of repeat units) in the precursor results in an increased disorder degree of carbon structure in the derived CMS membranes. The CMS membranes prepared by high FFV polyimide with helical chain conformation showed the looser carbon structure that are beneficial to CO2 transport compared with that prepared by polyimide with rod-like chain conformation. The larger size of the pendant functional groups (i.e. V-(CF3)2 > V-(CH3)2) in polyimide results in higher CO2 permeability of the derived CMS membranes. The BDAF-PMDA derived CMS membrane pyrolyzed at 700 °C show a high CO2 permeability (0.1 MPa of 50/50 mol.% mixed gas feed) of about 3000 Barrer and moderate CO2/CH4 selectivity, which exhibit an attractive application prospect for CO2 separation.
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