Amino-functionalized ZIFs-based porous liquids with low viscosity for efficient low-pressure CO2 capture and CO2/N2 separation

粘度 沸石咪唑盐骨架 多孔性 化学 吸附 化学工程 体积热力学 材料科学 分析化学(期刊) 色谱法 热力学 有机化学 复合材料 金属有机骨架 吸附 物理 工程类
作者
Xiaoqian Li,Dongdong Yao,Dechao Wang,Zhongjie He,Xiaolu Tian,Yangyang Xin,Fangfang Su,Hongni Wang,Jing Zhang,Xiaoyang Li,Mingtao Li,Yaping Zheng
出处
期刊:Chemical Engineering Journal [Elsevier BV]
卷期号:429: 132296-132296 被引量:45
标识
DOI:10.1016/j.cej.2021.132296
摘要

Construct permanent porosity into liquids remains challenging, such as preparation, lower viscosity, economical, high-performance gas sorption, and separation. Herein, a general and economical surface engineering strategy has been implemented to construct a novel type Ⅰ porous liquids based on zeolitic imidazolate frameworks (denoted as ZIFs-based PLs) via covalently linking of amino-functionalized ZIFs with the diglycidyl ether-terminated of PDMS. The properties including free pore volume, viscosity, melting temperature (Tm), the gas capture, and CO2/N2 selective separation performance of PLs can be regulated by adjusting the pore structures, the amount of –NH2 introduced into ZIFs and molecular weight of the outer layers of PDMS, etc. Particularly, PLs1(1000)-5%, and PLs2(1000)-5% present viscosity values with 49 mPa⋅S-1 and 59 mPa⋅S-1 at 25 °C, to our best knowledge, which is the lowest viscosity of type I PLs reported previously. Meanwhile, Tm of PLs broke down to −78 °C, showing a wide liquid range. Remarkably, type Ⅰ PLs1(14000)-15.5% exhibits approximately 10 times higher CO2 uptake than that of the polymer in outer layers, which is attributed to the permanent free volume of ZIFs, chemistry sorption, and excellent liquidity. The CO2 breakthrough time of PLs for the CO2/N2 mixture was delayed for 53.7 s, confirming that PLs exhibits efficient CO2/N2 separation performance. Therefore, we envision that such a general and economical strategy will open new insights to construct innovative low viscosity type Ⅰ PLs with high-performance CO2 capture and CO2/N2 separation at low pressure.
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