详细信息
Thin-film composite membrane improved by modified structure rearrangement process (mSRP) for rapidly aqueous and solvents separation ( SCI-EXPANDED收录 EI收录)
文献类型:期刊文献
英文题名:Thin-film composite membrane improved by modified structure rearrangement process (mSRP) for rapidly aqueous and solvents separation
作者:Chen, Bai-He[1];Deng, Hao-Ze[1];Han, Rui[2];Zhu, Man[1];Pan, Rui-Wen[1];Zhang, Xue-Wei[1];Xu, Zhen-Liang[2,3];Li, Hong-Bo[1];Xu, Sun-Jie[1,2,3]
机构:[1]East China Univ Sci & Technol, Sch Mat Sci & Engn, 130 Meilong Rd, Shanghai 200237, Peoples R China;[2]East China Univ Sci & Technol, Chem Engn Res Ctr, Sch Chem Engn, State Key Lab Chem Engn,Membrane Sci & Engn R&D La, Shanghai 200237, Peoples R China;[3]East China Univ Sci & Technol, Shanghai Elect Chem Innovat Inst, Shanghai 200237, Peoples R China
年份:2025
卷号:726
外文期刊名:JOURNAL OF MEMBRANE SCIENCE
收录:;EI(收录号:20251418169800);WOS:【SCI-EXPANDED(收录号:WOS:001462972000001)】;
基金:The authors gratefully acknowledge for the financial support received from National Natural Science Foundation of China (22208101) and Project funded by State Key R & D Program of China (2021YFB3801101 and 2021YFB3801103) as well as the research funding provided by the Fundamental Research Funds for the Central Universities (JKA01241502) .
语种:英文
外文关键词:Modified structure rearrangement process (mSRP); Host-guest interactions (HG); Organic solvent nanofiltration (OSN); 3-Amino-1-adamantanol (AAMO); Erythromycin (ERY)
摘要:This study aims to develop an advanced organic solvent nanofiltration (OSN) membrane by incorporating an adamantane-amide active layer through a modified structure rearrangement process (mSRP) combined with host-guest interactions. The membrane was fabricated by treating a commercial reverse osmosis (RO) membrane with solutions containing polysaccharides and adamantane monomers, obtaining significantly enhanced separation performance. The modified membrane exhibited a "mesh-like" morphology and increased surface roughness which contributed to substantially higher permeability and retention rates compared to those of pristine RO membrane. Specifically, the optimal membrane attained a permeability of 9.3 L m-2 h-1 & sdot;bar-1, representing an increase by 111.4 % relative to the pristine membrane, while maintaining a rejection rate of 94.0 % for the commonly used erythromycin antibiotic. The rearrangement behavior and mechanism of the host-guest interactions were investigated using density functional calculations. Long-term operational tests confirmed the stability of the membrane and its potential for industrial applications. This study introduced a novel approach for upgrading commercial RO membranes for efficient OSN applications, thereby contributing to the development of sustainable separation technologies in the biomedical sector.
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