Solvent-resistant polyimide aerogel film as ultrapermeable support for thin-film composite and covalent organic framework nanofiltration membranes

纳滤 气凝胶 聚酰亚胺 化学工程 材料科学 有机溶剂 薄膜复合膜 共价键 溶剂 共价有机骨架 高分子化学 复合数 有机化学 复合材料 化学 反渗透 图层(电子) 生物化学 工程类
作者
Jiahui Hu,Sushil Kumar,Rifan Hardian,Yang Cong,György Székely
出处
期刊:Separation and Purification Technology [Elsevier]
卷期号:302: 122162-122162 被引量:23
标识
DOI:10.1016/j.seppur.2022.122162
摘要

• A polyimide aerogel was applied as a versatile support for TFC and COF nanofiltration membranes. • Solvents and temperature affected the performance of the COF@aerogel membrane. • The pore flow model described the separation performance of the COF@aerogel membrane. • Stable performance was achieved under continuous, crossflow filtration for more than 9 days. • The polyimide aerogel support exhibited superior solvent resistance up to 6 months. Organic solvent nanofiltration (OSN) membranes require robust selective layers and support materials. In this study, polyamide and polyester thin-film composites (TFCs) and covalent organic frameworks (COFs) were fabricated as selective layers on a polyimide aerogel support. The ultrapermeable support was stable in various organic solvents including harsh polar aprotic solvents such as N,N-dimethylformamide, dimethylsulfoxide, N,N-dimethylacetamide, and N-methyl-2-pyrrolidone for more than six months. The support enabled fabricating both amorphous and crystalline selective layers at both room and higher temperatures. Moreover, the polyimide aerogel support had 85% porosity, facilitating high solvent flux. The compatibility of the selective layers and support was excellent, and as low molecular weight cutoff values (MWCO) as 356 and as high as 591 g mol −1 were obtained in methanol at 10 bar for the COFs and polyester TFC membranes, respectively. Both experimental MWCO and permeance values of the COF membrane agreed with those predicted using the pore flow model. The effect of the operating temperature on the OSN performance was examined in DMF at 20 and 100 °C. Both membranes demonstrated constant permeance and rejection for more than nine days of continuous filtration.
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