Task-Specific Ionic Liquids Tuning ZIF-67/PIM-1 Mixed Matrix Membranes for Efficient CO2 Separation

被引:41
|
作者
Han, Jiuli [1 ,2 ]
Bai, Lu [1 ,3 ]
Jiang, Haiyan [1 ,4 ]
Zeng, Shaojuan [1 ]
Yang, Bingbing [1 ,2 ]
Bai, Yinge [1 ]
Zhang, Xiangping [1 ,2 ]
机构
[1] Chinese Acad Sci, Inst Proc Engn, Beijing Key Lab Ion Liquids Clean Proc, CAS Key Lab Green Proc & Engn,State Key Lab Multi, Beijing 100190, Peoples R China
[2] Univ Chinese Acad Sci, Sch Chem Engn, Beijing 100049, Peoples R China
[3] Chinese Acad Sci, Innovat Acad Green Manufacture, Beijing 100190, Peoples R China
[4] Univ Chinese Acad Sci, Sch Future Technol, Beijing 100049, Peoples R China
基金
国家重点研发计划; 中国国家自然科学基金;
关键词
INTRINSIC MICROPOROSITY PIM-1; GAS SEPARATION; COMPOSITE MEMBRANES; BLEND MEMBRANES; POLYMERS; FRAMEWORK; FABRICATION; CHALLENGES; MMMS;
D O I
10.1021/acs.iecr.0c04830
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Ionic liquids (ILs) have become attractive in membranes for CO2 separation because of the designable structure, high CO2 affinity, and good compatibility and stability. Modification of metal-organic frameworks with ILs is an effective strategy to improve the gas separation performance of mixed matrix membranes (MMMs). In this work, task-specific ionic liquids (TSILs) were incorporated to prepare TSIL@ZIF-67/PIM-1 MMMs and improve CO2 separation performance because of the high CO2 solubility and great compatibility toward ZIF-67 and PIM-1. The TSILs (TMGHIM and TMGHPhO) selectively and reversibly interact with CO2 and improve the interfacial compatibility between ZIF-67 and PIM-1, leading to higher CO2/CH4 and CO2/N-2 selectivities than that of the ZIF-67/PIM-1 MMM and the directly blended membrane (TSIL/ZIF-67/PIM-1). The 10 wt % TMGHIM@ZIF-67/PIM-1 MMM shows enhanced CO2/N-2 and CO2/CH4 selectivities of 13.7 and 10.5, respectively; meanwhile, the CO2 permeability reaches 12,848.5 Barrer and is 2.5 times that of the pure PIM-1 membrane. The TSIL@ZIF-67/PIM-1 MMMs also show good stability against physical aging.
引用
收藏
页码:593 / 603
页数:11
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