膜
化学工程
PEG比率
渗透
溶解度
材料科学
气体分离
聚乙二醇
高分子化学
溶剂
乙醚
化学
有机化学
工程类
生物化学
经济
财务
作者
Tarik Eljaddi,Julien Bouillon,Denis Roizard,Laurent Lebrun
出处
期刊:Membranes
[Multidisciplinary Digital Publishing Institute]
日期:2022-08-27
卷期号:12 (9): 836-836
被引量:7
标识
DOI:10.3390/membranes12090836
摘要
A series of mixed matrix membranes containing poly (ether-block-amide) Pebax 1657 as matrix and polyethylene glycol (PEG) and Zeolitic Imidazolate Framework-8 (ZIF-8) as additives, were prepared and tested for CO2 separation. The membranes were prepared by solvent evaporation method and were characterized by TGA, DSC, SEM, and gas permeation measurements. The effects of PEG and its molecular weight, and the percentage of ZIF-8 into Pebax matrix were investigated. The results showed that the addition of PEG to Pebax/ZIF-8 blends avoid the agglomeration of ZIF-8 particles. A synergic effect between PEG and ZIF was particularly observed for high ZIF-8 content, because the initial permeability of pristine Pebax was multiplied by three (from 54 to 161 Barrers) while keeping the CO2 selectivity (αCO2/N2 = 61, αCO2/CH4 = 12 and αCO2/O2 = 23). Finally, the mechanism of CO2 transport is essentially governed by the solubility of CO2 into the membranes. Therefore, this new Pebax/PEG/ZIF-8 system seems to be a promising approach to develop new selective membranes for CO2 with high permeability.
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