膜
缩水甘油醚
高分子化学
二胺
乙二醇
乙醚
渗透
化学工程
离子液体
化学
亚乙基二氧
PEG比率
离子载体
溶剂
气体分离
热稳定性
材料科学
有机化学
双酚A
环氧树脂
烷基
生物化学
财务
经济
工程类
催化作用
作者
Zhongde Dai,Luca Ansaloni,Douglas L. Gin,Richard D. Noble,Liyuan Deng
标识
DOI:10.1016/j.memsci.2016.10.026
摘要
In this study, a new family of poly(ethylene glycol) (PEG)-based membranes for CO2 separation was developed using PEG diglycidyl ether (PEGDE) cross-linked with a low-molecular-weight diamine (2,2′-(ethylenedioxy)bis(ethylamine)) and a polyamine-based ionic liquid (triethylenetetramine trifluoroacetate, [TETA][Tfa]) in a solvent-free process. A mass fraction up to 80% PEG dimethyl ether (PEGDME, average Mn~250) was added to the cross-linked matrix to enhance the gas transport properties. The cross-linking reaction mechanism, thermal stability of the resulting membranes, as well as water uptakes of the formed membranes were systematically investigated. The CO2, N2, and CH4 gas transport properties of these new membranes were studied. Both CO2/N2 and CO2/CH4 binary mixed gas separation performances of the membranes at various humidity levels were tested. The gas permeation results showed that the free PEGDME additive acts as plasticizer in the polymeric matrix, resulting in excellent CO2/ N2 and CO2/CH4 separation properties.
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