DOI: 10.18174/443551
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Desalination with porous electrodes : Mechanisms of ion transport and adsorption

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Cited by 3 publications
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“…Another informative way to present the breakdown of energy consumption in CDI and MCDI processes is to plot cumulative specific energy consumptions as a function of σ for the full charging/discharge cycle (Figure 3C,D), similar to what has been shown by Dykstra et al 76,77 Surprisingly, even though the charge efficiency of MCDI is higher than that of CDI, SEC of the two processes, both achieving the same separation and with the same current density, are very similar (without considering possible Faradaic reactions). This may be explained by the fact that the additional ΔV D,mem and ΔV i,mem in MCDI is offset by the significant reduction of ΔV i,mA due to the much higher macropore concentration enabled by the IEMs.…”
Section: ■ Thermodynamic Energy Efficiencymentioning
confidence: 76%
“…Another informative way to present the breakdown of energy consumption in CDI and MCDI processes is to plot cumulative specific energy consumptions as a function of σ for the full charging/discharge cycle (Figure 3C,D), similar to what has been shown by Dykstra et al 76,77 Surprisingly, even though the charge efficiency of MCDI is higher than that of CDI, SEC of the two processes, both achieving the same separation and with the same current density, are very similar (without considering possible Faradaic reactions). This may be explained by the fact that the additional ΔV D,mem and ΔV i,mem in MCDI is offset by the significant reduction of ΔV i,mA due to the much higher macropore concentration enabled by the IEMs.…”
Section: ■ Thermodynamic Energy Efficiencymentioning
confidence: 76%
“…One of the most effective strategies to keep a high desalination performance is the inclusion of IEMs in the CDI cell, a cell design we refer to as MCDI. These IEMs are placed in front of the electrodes and contribute to maintaining the desalination performance in two ways: the membranes effectively slow down the transport of dissolved oxygen to the electrodes and consequently limit the rate of carbon oxidation and the related pH changes. , However, during long-term operation, dissolved oxygen will eventually oxidize the electrically positively polarized electrode (anode), and oxygen-containing surface groups will form. , Whereas these groups would have negatively affected the desalination performance in CDI (without membranes) due to enhanced coion expulsion during desalination, in MCDI, the desalination performance does not decline because IEMs prevent coions from leaving the electrode region. , Furthermore, Faradaic reactions during MCDI operation were also confirmed in our previous work by microscopic physics-based modeling of pH changes . This study predicted only minor pH changes during desalination in MCDI when non-Faradaic processes, including the effect of different mobilities of various ions on transport rates, combined with acid–base reactions and the presence of chemical surface groups in the micropores are taken into account.…”
Section: Introductionmentioning
confidence: 99%
“…A CDI unit comprises two porous electrodes (often carbon electrodes) and a separator (either a porous dielectric material or an open channel) [ 26 ]. Typically, the electrodes are treated to a potential difference of 1–1.4 V [ 27 ]. The saline or contaminated water passes between the positive and negative electrodes, where the unwanted ions in the water move into an electric double layer (EDL) along the electrode–water interface, thereby removing the unwanted salts or contaminants [ 28 ] via electrosorption on the electrode surfaces ( Figure 1 a).…”
Section: Introductionmentioning
confidence: 99%