On-site affordable acid and base production from seawater using bipolar membrane electrodialysis: ion transport and polyelectrolyte multilayer coating

The ability to produce acids and bases on-site at low energy and cost is of great interest to seawater reverse osmosis desalination plants. An acid is needed to lower the seawater pH to mitigate scaling in reverse osmosis (RO) modules. A base is needed to shift the boron equilibrium in the permeate of the first RO stage towards borate, which can then be rejected by the membrane in a second RO stage. We investigated the direct use of synthetic seawater in a bipolar membrane electrodialysis (BMED) process to produce acids and bases on-site. When synthetic seawater was used in a conventional BMED stack, Mg(OH) 2 scaling occurred inside the BMED stack, specifically in the salt compartments and the cation-exchange membranes (CEMs). The scaling resulted in a decline in current efficiency and raised the energy consumption of the BMED stack compared to using a pure NaCl stream. To mitigate the scaling, we used CEMs coated with a PAH/PSS multilayer to limit the transport of multivalent cations from the salt to the base compartment. Moreover, the salt compartment was acidified with a fraction of the produced protons to prevent the precipitation of Mg 2+ and Ca 2+ . In the first run, the modified BMED stack successfully produced a 0.2 M OH − and a 0.2 M H + solution at 85 % current efficiency and 0.05 kWh/mol OH − . However, repeated operation showed a gradual decline in performance due to OH − leakage through the CEM. To ensure long-term process stability, CEMs with improved OH − retention must be developed for the BMED application. • We analyzed the current and energy efficiency of bipolar membrane electrodialysis. • The current efficiency was limited by co-ion leakages across the monopolar membranes. • Mg(OH) 2 scaling is the bottleneck for using seawater in BMED stacks. • Magnesium scaling occurred in the salt compartment and the cation-exchange membrane. • Mg 2+ ions were not detected in the base reservoir.

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Publication Details

Journal
Desalination
Published
2025-12-24
DOI
https://doi.org/10.1016/j.desal.2025.119788
Primary Topic
Membrane-based Ion Separation Techniques
Type
article
Field-Weighted Citation Impact
0.00

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article

On-site affordable acid and base production from seawater using bipolar membrane electrodialysis: ion transport and polyelectrolyte multilayer coating

Alaaeldin A.E. Elozeiri, Jouke E. Dykstra, Huub H.M. Rijnaarts, Rob G.H. Lammertink et al.
Desalination
Membrane-based Ion Separation Techniques
article

On-site affordable acid and base production from seawater using bipolar membrane electrodialysis: ion transport and polyelectrolyte multilayer coating

Alaaeldin A.E. Elozeiri, Jouke E. Dykstra, Huub H.M. Rijnaarts, Rob G.H. Lammertink, Dean Spasov
article en

Abstract

The ability to produce acids and bases on-site at low energy and cost is of great interest to seawater reverse osmosis desalination plants. An acid is needed to lower the seawater pH to mitigate scaling in reverse osmosis (RO) modules. A base is needed to shift the boron equilibrium in the permeate of the first RO stage towards borate, which can then be rejected by the membrane in a second RO stage. We investigated the direct use of synthetic seawater in a bipolar membrane electrodialysis (BMED) process to produce acids and bases on-site. When synthetic seawater was used in a conventional BMED stack, Mg(OH) 2 scaling occurred inside the BMED stack, specifically in the salt compartments and the cation-exchange membranes (CEMs). The scaling resulted in a decline in current efficiency and raised the energy consumption of the BMED stack compared to using a pure NaCl stream. To mitigate the scaling, we used CEMs coated with a PAH/PSS multilayer to limit the transport of multivalent cations from the salt to the base compartment. Moreover, the salt compartment was acidified with a fraction of the produced protons to prevent the precipitation of Mg 2+ and Ca 2+ . In the first run, the modified BMED stack successfully produced a 0.2 M OH − and a 0.2 M H + solution at 85 % current efficiency and 0.05 kWh/mol OH − . However, repeated operation showed a gradual decline in performance due to OH − leakage through the CEM. To ensure long-term process stability, CEMs with improved OH − retention must be developed for the BMED application. • We analyzed the current and energy efficiency of bipolar membrane electrodialysis. • The current efficiency was limited by co-ion leakages across the monopolar membranes. • Mg(OH) 2 scaling is the bottleneck for using seawater in BMED stacks. • Magnesium scaling occurred in the salt compartment and the cation-exchange membrane. • Mg 2+ ions were not detected in the base reservoir.

DesalinationVol. 623
Wageningen University & Research (NL), University of Twente (NL)
Nederlandse Organisatie voor Wetenschappelijk Onderzoek, Wageningen University and Research
Affordable and clean energy
Openalex Percentile: Top 43%
Membrane-based Ion Separation Techniques
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