Water trapping inside anion exchange membranes during practical reverse electrodialysis applications

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 (~0.9 M NaClequivalent) and underground water (~0.01 M NaClequivalent). The net power and net energy efficiency were initially 1.8 W m−2cell pair 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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Publication Details

Journal
npj Clean Water
Published
2024-09-13
DOI
https://doi.org/10.1038/s41545-024-00381-y
Citations
2
Primary Topic
Membrane-based Ion Separation Techniques
Type
article
Field-Weighted Citation Impact
0.37

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article

Water trapping inside anion exchange membranes during practical reverse electrodialysis applications

Nam Jo Jeong, Young Sun Mok, SeungCheol Yang, Dong-Gun Lee et al.
2 citations
npj Clean Water
Membrane-based Ion Separation Techniques
0.37
article

Water trapping inside anion exchange membranes during practical reverse electrodialysis applications

Nam Jo Jeong, Young Sun Mok, SeungCheol Yang, Dong-Gun Lee, Jiyeon Choi, Hanki Kim, Ji-Hyung Han
article en
2 citations

Abstract

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 (~0.9 M NaClequivalent) and underground water (~0.01 M NaClequivalent). The net power and net energy efficiency were initially 1.8 W m−2cell pair 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.

npj Clean WaterVol. 7(1)
Changwon National University (KR), Korea Institute of Energy Research (KR), Jeju TechnoPark (KR), Jeju National University (KR)
Ministry of Science and ICT, South Korea
Clean water and sanitation
Openalex Percentile: Top 44%
Membrane-based Ion Separation Techniques
0.37
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