Pebax/TSIL blend thin film composite membranes for CO2 separation

被引:2
|
作者
Zhongde Dai [1 ]
Lu Bai [2 ]
Karoline N?vik Hval
Xiangping Zhang [2 ]
Suojiang Zhang [2 ]
Liyuan Deng [1 ]
机构
[1] Department of Chemical Engineering, Norwegian University of Science and Technology
[2] Beijing Key Laboratory of Ionic Liquids Clean Process
[3] Institute of Process Engineering, Chinese Academy of Sciences
关键词
CO2; capture; thin film composite membrane; task specific ionic liquids; Pebax; post combustion;
D O I
暂无
中图分类号
TQ028.8 [新型分离法];
学科分类号
081701 ; 081704 ;
摘要
In this study a thin film composite(TFC) membrane with a Pebax/Task-specific ionic liquid(TSIL) blend selective layer was prepared. Defect-free Pebax/TSIL layers were coated successfully on a polysulfone ultrafiltration porous support with a polydimethylsiloxane(PDMS) gutter layer. Different parameters in the membrane preparation(e.g. concentration, coating time) were investigated and optimized. The morphology of the membranes was studied by scanning electron microscopy(SEM), while the thermal properties and chemical structures of the membrane materials were investigated by thermo-gravimetric analyzer(TGA), differential scanning calorimetry(DSC) and Fourier transform infrared spectroscopy(FTIR). The CO2separation performance of the membrane was evaluated using a mixed gas permeation test. Experimental results show that the incorporation of TSIL into the Pebax matrix can significantly increase both CO2permeance and CO2/N2selectivity. With the presence of water vapor, the membrane exhibits the best CO2/N2selectivity at a relative humidity of around 75%, where a CO2permeance of around 500 GPU and a CO2/N2selectivity of 46 were documented. A further increase in the relative humidity resulted in higher CO2permeance but decreased CO2/N2selectivity. Experiments also show that CO2permeance decreases with a CO2partial pressure increase, which is considered a characteristic in facilitated transport membranes.
引用
收藏
页码:538 / 546
页数:9
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