Asymmetric sulfonated polysulfone cation exchange membranes prepared by non-solvent induced phase separation for reverse electrodialysis using desalination brines

The transition to sustainable energy is crucial for modern society, and Reverse Electrodialysis (RED) offers a promising method for harvesting energy from salinity gradients. However, large-scale deployment of RED is constrained by efficiency limitations and the high cost of ion exchange membranes. This study focuses on the development of novel asymmetric cation exchange membranes (CEMs) based on sulfonated polysulfone (SPSf) prepared via non-solvent induced phase inversion (NIPS). The highest degree of sulfonation achieved was 0.50, which optimized the balance between electrochemical membrane properties and the processability for CEMs preparation. CEMs properties were further fine-tuned by adjusting the polymer solution composition, with optimal performance achieved using a 20 wt% of 2-propanol as co-solvent in dimethylformamide. Electrochemical characterization under various saline conditions demonstrated favourable transport properties of the optimized CEMs. When tested in RED, the membrane achieved a maximum power density of 220 mW·m⁻² per cell pair under a 0.1 M/0.5 M NaCl gradient, comparable to commercial CEMs under similar conditions. These results highlight the potential of the developed membranes to advance RED technology, providing an economically viable and efficient solution for salinity gradient energy conversion.

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Publication Details

Journal
Electrochimica Acta
Published
2025-09-01
DOI
https://doi.org/10.1016/j.electacta.2025.147292
Citations
8
Primary Topic
Membrane-based Ion Separation Techniques
Type
article
Field-Weighted Citation Impact
5.39
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article

Asymmetric sulfonated polysulfone cation exchange membranes prepared by non-solvent induced phase separation for reverse electrodialysis using desalination brines

Marco Aquino, Giovanna Palermo, Sergio Santoro, Ahmet H. Avci et al.
8 citations
Electrochimica Acta
Membrane-based Ion Separation Techniques
5.39
article

Asymmetric sulfonated polysulfone cation exchange membranes prepared by non-solvent induced phase separation for reverse electrodialysis using desalination brines

Marco Aquino, Giovanna Palermo, Sergio Santoro, Ahmet H. Avci, Salvatore Straface, Mariano Davoli, Grazia Giuseppina Politano, Dante M. Aceti, Mauro Francesco La Russa, Efrem Curcio, Karel Bouzek, Antonio Politano, Ramato Ashu Tufa
article en
8 citations

Abstract

The transition to sustainable energy is crucial for modern society, and Reverse Electrodialysis (RED) offers a promising method for harvesting energy from salinity gradients. However, large-scale deployment of RED is constrained by efficiency limitations and the high cost of ion exchange membranes. This study focuses on the development of novel asymmetric cation exchange membranes (CEMs) based on sulfonated polysulfone (SPSf) prepared via non-solvent induced phase inversion (NIPS). The highest degree of sulfonation achieved was 0.50, which optimized the balance between electrochemical membrane properties and the processability for CEMs preparation. CEMs properties were further fine-tuned by adjusting the polymer solution composition, with optimal performance achieved using a 20 wt% of 2-propanol as co-solvent in dimethylformamide. Electrochemical characterization under various saline conditions demonstrated favourable transport properties of the optimized CEMs. When tested in RED, the membrane achieved a maximum power density of 220 mW·m⁻² per cell pair under a 0.1 M/0.5 M NaCl gradient, comparable to commercial CEMs under similar conditions. These results highlight the potential of the developed membranes to advance RED technology, providing an economically viable and efficient solution for salinity gradient energy conversion.

Electrochimica ActaVol. 541
Lund University (SE), University of L'Aquila (IT), Istituto di Nanotecnologia (IT), University of Calabria (IT), University of Chemistry and Technology, Prague (CZ)
Openalex Percentile: Top 4%
Membrane-based Ion Separation Techniques
5.39
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