Pervaporation Membrane for Linear Alpha Olefin Separation Using Surface-Activated Silver Nanoparticles as Carriers for Facilitated Transport

被引:0
|
作者
Seo, Yeon Woo [1 ,2 ]
Lim, Suim [3 ,4 ]
Park, Jin Woo [5 ]
Jeon, Wonjin [6 ]
Kim, Yong-Doo [6 ]
Lee, Kyong-Hwan [6 ]
Yim, Kanghoon [4 ]
Kim, Jong Hak [2 ]
Lee, Jung Hyun [1 ,2 ,3 ,4 ,6 ]
机构
[1] Korea Inst Energy Res, Hydrogen Convergence Mat Lab, Daejeon 34129, South Korea
[2] Yonsei Univ, Dept Chem & Biomol Engn, Seoul 03722, South Korea
[3] Sogang Univ, Dept Mech Engn, Seoul 04107, South Korea
[4] Korea Inst Energy Res, Energy AI & Computat Lab, Daejeon 34129, South Korea
[5] Korea Inst Energy Res, Energy Storage Dept, Daejeon 305343, South Korea
[6] Korea Inst Energy Res, Bioenergy & Resources Upcycling Res Lab, Daejeon 34129, South Korea
来源
ACS APPLIED ENGINEERING MATERIALS | 2024年 / 2卷 / 09期
关键词
facilitated olefin transport; Ag nanoparticles; surface positive charge; olefin separation; pervaporation; polymer membranes; density functional theory; POLYMER ELECTROLYTE MEMBRANES; OLEFIN/PARAFFIN SEPARATION; COMPLEX MEMBRANES; AG NANOPARTICLES; PERFORMANCE; OXYGEN; STABILITY; MIXTURES; MATRIX;
D O I
10.1021/acsaenm.4c00382
中图分类号
T [工业技术];
学科分类号
08 ;
摘要
Facilitated transport membranes provide a low-cost means of separating hydrocarbon mixtures. However, the application of such membranes is currently limited to gas-phase mixtures. In this study, a pervaporation membrane that can separate high concentrations of linear alpha olefins (e.g., 1-hexene and 1-octene) from liquid-phase hydrocarbon mixtures was developed. The pervaporation membrane was fabricated by coating a known olefin gas separation membrane material, poly(vinylpyrrolidone), onto a microporous support. Silver nanoparticles (Ag NPs) were incorporated into the polymer matrix and activated by the electron-accepting polarizer 7,7,8,8-tetracyanoquinodimethane to induce a partial positive charge on their surface. They acted as olefin carriers for facilitated transport, resulting in the extremely high pervaporative separation of a 1-hexene/n-hexane mixture over a long period. A 1-hexene concentration of more than 99% in the permeate was achieved at a feed concentration of 25%, resulting in a separation factor higher than 100 under stable operation for at least 100 h. Additionally, when the permeate pressure increased to 500 mbar, the 1-hexene flux sharply increased because of facilitated transport by the carrier action of the surface-charged Ag NPs, whereas the n-hexane flux remained nearly unchanged. These results demonstrate that facilitated transport membranes are highly effective in the pervaporative separation of liquid-phase mixtures and thus may provide a future direction for the development of high-performance membrane materials.
引用
收藏
页码:2285 / 2294
页数:10
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