2019
DOI: 10.1016/j.desal.2019.01.031
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An investigation of the impact of fouling agents in capacitive and membrane capacitive deionisation

Abstract: The effect of organic fouling on both capacitive deionization (CDI) and membrane capacitive deionization (MCDI) was studied using two model foulants, the sodium salt of alginic acid and humic acid. Fouling of the activated carbon electrodes in the CDI cell was significant. The salt adsorption fell to 75% and the charge efficiency to 90% of their initial values after 18 cycles of operation with 0.5 mM CaCl 2 and 60 mg L -1 of sodium alginate. Similarly, the salt adsorption fell to 70% and the charge efficiency … Show more

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Cited by 45 publications
(21 citation statements)
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“…Fouling in CDI mainly occurs on electrodes and results in a reduction in electrode conductivity, electro-sorption capacitance, and cell stability. Organic foulants reduce cell performance by blocking electrode pores, competing with ions for adsorption sites, hindering ion diffusion to the electrodes, and accelerating intercalation electrode dissolution [ 445 , 446 ]. The observed scaling issues are less severe than fouling in (M)CDI studies, which may be a result of the relatively low hardness of brackish water used in (M)CDI.…”
Section: Membrane Capacitive Deionizationmentioning
confidence: 99%
“…Fouling in CDI mainly occurs on electrodes and results in a reduction in electrode conductivity, electro-sorption capacitance, and cell stability. Organic foulants reduce cell performance by blocking electrode pores, competing with ions for adsorption sites, hindering ion diffusion to the electrodes, and accelerating intercalation electrode dissolution [ 445 , 446 ]. The observed scaling issues are less severe than fouling in (M)CDI studies, which may be a result of the relatively low hardness of brackish water used in (M)CDI.…”
Section: Membrane Capacitive Deionizationmentioning
confidence: 99%
“…No selectivity was found for STP effluent ( ̅ = 0.97; SD = 0.16; N = 4) while S could not be calculated for Eumes river water due to the lack of hardness ions. Preferential removal of bivalent ions is common in MCDI; it is observed in both synthetic feed mixtures [19,32] and real feed water [9]. This phenomenon is the result of diffusion kinetics and adsorption equilibria in MCDI and is attributed to the preferential storage of multivalent ions in ion exchange membranes [32,33].…”
Section: Cost Estimatementioning
confidence: 99%
“…MCDI is expected to be less prone to fouling and scaling than other membrane-based desalination technologies [18]. The membranes in MCDI protect the carbon electrodes [19] and due to frequent electrode reversal, build-up of fouling is prevented in a similar way to electrodialysis reversal [15]. MCDI is therefore a potentially highly interesting technology for cooling tower feed pretreatment.…”
Section: Introductionmentioning
confidence: 99%
“…The fouling phenomenon (electrode longevity) is another critical issue that needs to be addressed. Fundamental organic and inorganic fouling experiments have been reported for CDI and ED [ 112 , 113 , 114 , 115 , 116 ], but fouling phenomena are not yet fully understood, as electrochemical processes are in the early stages of research compared to membrane processes. Moreover, a limited number of operations with relatively short cycles (mostly <100) have been reported for electrochemical processes [ 80 , 85 , 86 , 87 ].…”
Section: Perspectives For Future Desalination and The Role Of Nanomentioning
confidence: 99%