TY - JOUR
T1 - Scale-Up Strategies for Redox-Mediated Electrodialysis for Desalination
T2 - The Role of Electrode and Channel Stacks
AU - Kim, Gamin
AU - Kim, Hyunjin
AU - Kim, Minhui
AU - Kim, Nayeong
AU - Lee, Byeongho
AU - Kim, Seonghwan
AU - Su, Xiao
AU - Kim, Choonsoo
N1 - This study was supported by a research grant from the Waste to Energy Recycling Human Resource Development Project of the Korean Ministry of the Environment (ME). This study was also supported by the Basic Science Research Program through the National Research Foundation of Korea (NRF) funded by the Ministry of Education (NRF\u20102021R1I1A3040360). This study was also supported by Basic Science Research Program through the National Research Foundation of Korea (NRF) funded by the Ministry of Education (no. RS\u20102024\u201000414203).
PY - 2025/4/7
Y1 - 2025/4/7
N2 - Redox-mediated electrodialysis (redox-ED) enhances the economic and energy feasibility of conventional electrodialysis by substituting water splitting and costly metal-basedelectrodes with reversible redox reactions and porous carbon electrodes. Despite growing interest, the development of scale-up strategies for redox-ED remains limited, delaying its industrial implementation. This study proposes a scale-up strategy by examining the impact of stacking electrodes and channels on the desalination performance of the system, aiming to enable economically viable desalination. The results show that electrode and channel stacking (up to three stacks) significantly enhances desalination performance, resulting in a 6.8-fold increase in the salt removal rate, and a 30% improvement in productivity. These enhancements can be attributed to synergistic effects of electrode and channel stacking, which improve the redox reaction rate by increasing the surface area and enhancing the system capacity by increasing the volumetric flow rate. Technoeconomic analysis underscores the economic viability of the scale-up strategy proposed in this study, showing 18% and 32% reductions in capital and operating costs, respectively, compared with multiple unit cell systems. Overall, incorporating multiple stacks of electrodes and channels offers an effective strategy for scaling up redox-ED systems with high economic viability, thereby providing a pathway for their industrial utilization.
AB - Redox-mediated electrodialysis (redox-ED) enhances the economic and energy feasibility of conventional electrodialysis by substituting water splitting and costly metal-basedelectrodes with reversible redox reactions and porous carbon electrodes. Despite growing interest, the development of scale-up strategies for redox-ED remains limited, delaying its industrial implementation. This study proposes a scale-up strategy by examining the impact of stacking electrodes and channels on the desalination performance of the system, aiming to enable economically viable desalination. The results show that electrode and channel stacking (up to three stacks) significantly enhances desalination performance, resulting in a 6.8-fold increase in the salt removal rate, and a 30% improvement in productivity. These enhancements can be attributed to synergistic effects of electrode and channel stacking, which improve the redox reaction rate by increasing the surface area and enhancing the system capacity by increasing the volumetric flow rate. Technoeconomic analysis underscores the economic viability of the scale-up strategy proposed in this study, showing 18% and 32% reductions in capital and operating costs, respectively, compared with multiple unit cell systems. Overall, incorporating multiple stacks of electrodes and channels offers an effective strategy for scaling up redox-ED systems with high economic viability, thereby providing a pathway for their industrial utilization.
KW - desalination
KW - redox-mediated electrodialysis
KW - scale-up
KW - sustainable chemistries
KW - water chemistries
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U2 - 10.1002/cssc.202500452
DO - 10.1002/cssc.202500452
M3 - Article
C2 - 40159438
AN - SCOPUS:105002158353
SN - 1864-5631
VL - 18
JO - ChemSusChem
JF - ChemSusChem
IS - 12
M1 - e202500452
ER -