Water trapping inside anion exchange membranes during practical reverse electrodialysis applications

被引:0
|
作者
Lee, Dong-Gun [1 ,2 ]
Kim, Hanki [1 ]
Yang, Seungcheol [3 ,4 ]
Han, Ji-Hyung [1 ]
Mok, Young Sun [5 ]
Jeong, Nam Jo [1 ]
Choi, Jiyeon [1 ,2 ]
机构
[1] Korea Inst Energy Res, Jeju Global Res Ctr, Jeju Si 695971, Jeju Special Se, South Korea
[2] Korea Inst Energy Res, Daejeon, South Korea
[3] Changwon Natl Univ, Dept Mat Convergence & Syst Engn, Changwon Si, Gyeongsangnam D, South Korea
[4] Changwon Natl Univ, Sch Mat Sci & Engn, Changwon Si 51140, Gyeongsangnam D, South Korea
[5] Jeju Natl Univ, Dept Chem & Biol Engn, Jeju Si, Jeju Special Se, South Korea
来源
NPJ CLEAN WATER | 2024年 / 7卷 / 01期
关键词
PLANCK TRANSPORT-THEORY; ENERGY GENERATION; POWER-GENERATION; PERFORMANCE; DENSITY; IONS; MG2+;
D O I
10.1038/s41545-024-00381-y
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The power output of reverse electrodialysis (RED), an important renewable energy technology, can be improved using high-salinity feed solutions. Herein, a RED stack of ultrathin ion exchange membranes was operated continuously for 10 days using reverse osmosis brine (similar to 0.9 M NaClequivalent) and underground water (similar to 0.01 M NaClequivalent). The net power and net energy efficiency were initially 1.8 W m(cell pair)(-2) and 40.8%, respectively, and then decreased gradually, as did the generated current and stack resistance. This deterioration was caused not by conventional membrane fouling but by trapped water inside the polymer matrix of the anion exchange membrane, especially near the cathode. The high salinity gradient and ultrathin membranes caused a flux imbalance between co-ion transport and osmotic water permeation. Further, bulk mass transfer was enhanced inside the RED stack to maintain electroneutrality. Therefore, combinations of membranes with high water permeability and permselectivity may be required to achieve stable RED operation.
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页数:11
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