Stepped enhancement of CO2 adsorption and separation in IL-ZIF-IL composites with shell-interlayer-core structure

被引:22
作者
Han, Guopeng [1 ]
Yu, Na [2 ]
Liu, Dahuan [1 ]
Yu, Guangren [2 ]
Chen, Xiaochun [2 ]
Zhong, Chongli [1 ,3 ]
机构
[1] Beijing Univ Chem Technol, State Key Lab Organ Inorgan Composites, Beijing 100029, Peoples R China
[2] Beijing Univ Chem Technol, Coll Chem Engn, Beijing Key Lab Membrane Sci & Technol, Beijing 100029, Peoples R China
[3] Tianjin Polytech Univ, State Key Lab Separat Membranes & Membrane Proc, Tianjin 300387, Peoples R China
基金
中国国家自然科学基金;
关键词
CO2; capture; composites; ionic liquids; separation; zeolitic imidazolate framework; METAL-ORGANIC FRAMEWORK; IONIC LIQUIDS; CARBON-DIOXIDE; SELECTIVE CAPTURE; POROUS MATERIALS; PORE-SIZE; FLUE-GAS;
D O I
10.1002/aic.17112
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Development of materials with excellent separation performance remains an ongoing challenge in separation science and technology. Herein, a novel strategy was proposed to gradually enhance gas separation performance in micro/nano-materials, by constructing a shell-interlayer-core structure using ionic liquid (triethylenetetramine lactate, [TETA]L) and zeolitic imidazolate framework (ZIF-8). Such structure includes outer [TETA]L shell, interlayer of ZIF-8, and inner [TETA]L core, endowing the composite with more evident molecular sieving separation for CO2 mixtures than the reported materials. A high CO2 adsorption amount (1.53 mmol/g at 298 K and 1.0 bar) is maintained, while the uptakes for CH4 and N-2 are very low. Corresponding ideal adsorbed solution theory selectivities are 260-1,990 and 1,688-5,572 for CO2/CH4 and CO2/N-2 mixtures at the range of tested pressures. In addition, the separation performance can be controlled by varying the shell-interlayer-core structure with IL inside, outside or on both sides of ZIF-8 and the thickness of outer shell.
引用
收藏
页数:8
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