COF-anchored design of nanoporous graphene membranes for ultrafast and selective organic separation

被引:3
|
作者
Han, Xiao [1 ,2 ,4 ]
Ma, Liang [1 ]
Zhang, Shengping [1 ,2 ,4 ]
Zeng, Haiou [1 ]
Song, Ruiyang [1 ]
Wu, Ningran [1 ,2 ,4 ]
Liu, Yuancheng [1 ]
Duan, Hongwei [1 ,2 ]
Peng, Hailin [2 ,3 ,4 ]
Zhang, Sui [5 ]
Wang, Luda [1 ,2 ,4 ,6 ]
机构
[1] Peking Univ, Sch Integrated Circuits, Natl Key Lab Adv Micro & Nano Manufacture Technol, Beijing 100871, Peoples R China
[2] Peking Univ, Acad Adv Interdisciplinary Studies, Beijing 100871, Peoples R China
[3] Peking Univ, Coll Chem & Mol Engn, Beijing 100871, Peoples R China
[4] Beijing Graphene Inst, Technol Innovat Ctr Graphene Metrol & Standardizat, Beijing 100095, Peoples R China
[5] Natl Univ Singapore, Dept Chem & Biomol Engn, Singapore 117576, Singapore
[6] Beijing Adv Innovat Ctr Integrated Circuits, Beijing 100871, Peoples R China
基金
中国国家自然科学基金;
关键词
Atomically thin membranes; Nanoporous graphene; Covalent organic frameworks; Organic solvent recovery; Organic solvent forward osmosis; RAMAN-SPECTROSCOPY; INTRINSIC DEFECTS; SINGLE-LAYER; TRANSPORT; PERMEATION; WATER; NANOFILTRATION; FRAMEWORKS; HYBRID;
D O I
10.1016/j.memsci.2024.122689
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Nanoporous graphene has attracted extensive attention as a type of disruptive membrane materials for organic separation. However, the fabrication of an ideal graphene membrane with high permeability and selectivity remains challenging due to the inevitable non-selective defects. Here, a strategy based on synergetic effect of graphene membranes and covalent organic framework (COF) nanounits is developed. Atomically thin nanoporous graphene provides high solvent flux and stability. To prevent the leakage from inevitable non-selective pores in graphene without sacrificing flux, porous COF nanounits are directly anchored at the defective sites. The fabricated membranes exhibit record-high solvent flux of 49.81 L m- 2 h-1 (1-2 orders of magnitude higher than that of state-of-the-art membranes), and relatively low reverse solute flux of 1.69 g m- 2 h-1 in organic solvent forward osmosis (OSFO) process. The strategy we proposed gives dramatic impetus to the development of OSFO and other membrane separation processes.
引用
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页数:10
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