Poly(amphoteric)-Functionalized MXene Nanosheets to Construct Mixed-Matrix Membranes for Efficient Humidified CO2 Separation

被引:0
|
作者
Xin, Qingping [1 ]
Huang, Tao [1 ]
Li, Shuo [1 ]
Gao, Ningning [2 ]
Jin, Huimin [1 ]
Chen, Hao [1 ]
Zhang, Lei [3 ]
Ye, Hui [1 ]
Li, Hong [1 ]
Zhang, Yuzhong [1 ]
机构
[1] Tiangong Univ, Sch Mat Sci & Engn, State Key Lab Separat Membranes & Membrane Proc, Tianjin 300387, Peoples R China
[2] SINOPEC Res Inst Petr Proc Co Ltd, Natl Engn Res Ctr Petr Refining Technol & Catalyst, Beijing 100083, Peoples R China
[3] Tianjin Univ Sci & Technol, Tianjin Key Lab Brine Chem Engn & Resource Ecoutil, Tianjin 300457, Peoples R China
来源
ACS APPLIED POLYMER MATERIALS | 2024年 / 6卷 / 21期
关键词
XLPEO; MXene nanosheets; polyzwitterion; gas separation membrane; solubility diffusion mechanism; PERFORMANCE; ADSORPTION; MICROSPHERES;
D O I
10.1021/acsapm.4c02890
中图分类号
T [工业技术];
学科分类号
08 ;
摘要
The membrane separation approach has garnered considerable interest in the area of CO2 separation due to its advantages of requiring little electricity and a wide range of applications. Here, we report the preparation of pSBMA@Ti3C2T x nanosheets functionalized with poly(amphiphilic poly(methacryloyloxyethylsulfobetaine) (pSBMA)) by precipitation distillation, weighing of pSBMA@Ti3C2T x nanosheets with different mass ratios to be added into cross-linked poly(ethylene oxide) (XLPEO), and preparation of a continuous, thin mixed-matrix membrane (MMM). Under gas humidification, the membrane showed the best permeation performance. Due to the richness of hydrophilic organosulfate groups (-SO3 -) and quaternary amine groups [-N+(CH3)3] in pSBMA, the overall water content of the MMMs is increased, which greatly improves the CO2 permeability. Enhancing the ratio of bound water augments the membrane's capacity to segregate CO2/N2. Under coordination of water molecules, quaternary amine groups effectively promote the quick delivery of CO2 in the membrane. In the wet state, the XLPEO/pSBMA@Ti3C2T x -0.2 membrane has a CO2/N2 selectivity of 27.5 and a CO2 permeability of 4953 barrer, an improvement of 87% and 109%, respectively, compared to those of the XLPEO pure membrane, breaking the 2008 Robeson upper limit and approaching the 2019 upper limit. We also studied the change of the gas separation performance of the membrane under different pressures.
引用
收藏
页码:13413 / 13426
页数:14
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