Please use this identifier to cite or link to this item: https://hdl.handle.net/10356/147441
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dc.contributor.authorTang, Kexinen_US
dc.contributor.authorZhou, Kunen_US
dc.date.accessioned2021-04-05T04:05:31Z-
dc.date.available2021-04-05T04:05:31Z-
dc.date.issued2020-
dc.identifier.citationTang, K. & Zhou, K. (2020). Water desalination by flow-electrode capacitive deionization in overlimiting current regimes. Environmental Science and Technology, 54(9), 5853-5863. https://dx.doi.org/10.1021/acs.est.9b07591en_US
dc.identifier.issn0013-936Xen_US
dc.identifier.other0000-0001-9147-7995-
dc.identifier.urihttps://hdl.handle.net/10356/147441-
dc.description.abstractSince flow-electrodes do not have a maximum allowable charge capacity, a high salt removal rate in flow-electrode capacitive deionization (FCDI) can be achieved theoretically by simply increasing the applied voltage. However, present attempts to run FCDI at high voltages are unsatisfactory because of the instability of the module occurring in the overlimiting current regimes. To implement FCDI in the overlimiting current regimes (namely, OLC-FCDI), in this work, we analyzed the voltage-current (V-I) characteristics of several FCDI units. We confirmed that a continuous, rapid, and stable desalination performance of OLC-FCDI can be attained when the employed FCDI unit possesses a linear V-I characteristic (only one ohmic regime), which is distinct from the three V-I regimes in electrodialysis (ohmic, limiting current, and water splitting regimes) and the two in membrane capacitive deionization (ohmic and water splitting regimes). Notably, the linearV-I characteristic of FCDI requires continuous charge percolation near the boundaries of ion-exchange membranes. Effective methods include increasing the carbon content in the flow-electrodes and introducing electrical (carbon cloth) or ionic (ion-exchange resins) conductive intermediates in the solution compartment, which result in corresponding upgraded FCDI units exhibiting extremely high salt removal rates (>100 mg m-2 s-1), good cycling stability, and rapid seawater desalination performance under typical OLC-FCDI operation condition (27-40 g L-1 NaCl, 500 mA). This study can guide future research of FCDI in terms of flow-electrode preparation and device configuration optimization.en_US
dc.language.isoenen_US
dc.relation.ispartofEnvironmental Science and Technologyen_US
dc.rights© 2020 American Chemical Society (ACS). All rights reserved.en_US
dc.subjectEngineering::Environmental engineeringen_US
dc.titleWater desalination by flow-electrode capacitive deionization in overlimiting current regimesen_US
dc.typeJournal Articleen
dc.contributor.schoolSchool of Mechanical and Aerospace Engineeringen_US
dc.contributor.researchNanyang Environment and Water Research Instituteen_US
dc.identifier.doi10.1021/acs.est.9b07591-
dc.identifier.pmid32271562-
dc.identifier.scopus2-s2.0-85084270792-
dc.identifier.issue9en_US
dc.identifier.volume54en_US
dc.identifier.spage5853en_US
dc.identifier.epage5863en_US
dc.subject.keywordsWater Desalinationen_US
dc.subject.keywordsFlow-electrode Capacitive Deionizationen_US
item.fulltextNo Fulltext-
item.grantfulltextnone-
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