Biphenyl-based covalent triazine framework-incorporated polydimethylsiloxane membranes with high pervaporation performance for n-butanol recovery

被引:28
|
作者
Lee, Ju Yeon [1 ]
Park, Hongjin [2 ]
Lee, Jong Suk [3 ]
Yoon, Sungho [2 ]
Lee, Jung-Hyun [1 ]
机构
[1] Korea Univ, Dept Chem & Biol Engn, 145 Anam Ro, Seoul 02841, South Korea
[2] Chung Ang Univ, Dept Chem, 84 Heukseok Ro, Seoul 06974, South Korea
[3] Sogang Univ, Dept Chem & Biomol Engn, 35 Baekbeom Ro, Seoul 04107, South Korea
基金
新加坡国家研究基金会;
关键词
Pervaporation; Polydimethylsiloxane; Covalent triazine framework; Mixed matrix membranes; Butanol recovery; MIXED MATRIX MEMBRANES; MCM-41 SILICA SPHERES; HYBRID MEMBRANES; ETHANOL RECOVERY; AQUEOUS-SOLUTION; PDMS MEMBRANES; SEPARATION; SURFACE; ZEOLITE; ACETONE;
D O I
10.1016/j.memsci.2019.117654
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Biphenyl-based covalent triazine framework (CTF) particles, as a new class of organic porous materials, were incorporated into polydimethylsiloxane (PDMS) for the fabrication of a high performance pervaporation membrane for n-butanol (n-BtOH) recovery. Increasing the CTF loading remarkably enhanced both the flux and the separation factor of the membrane. This was ascribed to the strongly hydrophobic, highly porous and mesoporous structure of CTF providing highly permeable and preferential pathways for n-BtOH. Importantly, compared to other reported PDMS-based mixed matrix membranes containing conventional microporous particles, our CTF-incorporated PDMS (CTF/PDMS) membrane exhibited a significantly higher flux and excellent separation factor. Increasing feed temperature and n-BtOH concentration further enhanced pervaporation performance. As a result, the maximum n-BtOH recovery performance (total permeate flux: 2816 +/- 118 g m(-2) h(-1), separation factor: 62.8 +/- 1.5 and permeate n-BtOH concentration: 71.5 +/- 2.7 wt%) was attained when the CTF/PDMS membrane containing 12.5 wt% CTF was operated with a 4 wt% n-BtOH feed solution at 60 degrees C. Our proposed strategy provides an effective method to prepare high performance membranes for pervaporation and gas and organic solvent separation.
引用
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页数:10
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