2016
DOI: 10.1038/nchem.2466
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Redox flow batteries go organic

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Cited by 120 publications
(77 citation statements)
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“…[12,13] In the last few years, RFBs based on organic redox molecules, such as quinones, phenothiazine, nitroxides, viologens, and pyridines [14][15][16][17] have experienced a great deal of interest, becoming one of the hottest topics in electrochemical energy storage (see Table S1 in the Supporting Information). [18,19] Regardless of the chemical nature of the electroactive species and the type of electrolytes, most RFBs rely on ion-selective membranes to separate the two redox electrolytes and to prevent the crossover of active compounds while allowing the migration of charge carriers. It is worth mentioning that membranes are not employed in some hybrid RFBs in which one of the active species is a solid, such as Zn, [20,21] Cd, [22] lithium, [23] or graphite.…”
mentioning
confidence: 99%
“…[12,13] In the last few years, RFBs based on organic redox molecules, such as quinones, phenothiazine, nitroxides, viologens, and pyridines [14][15][16][17] have experienced a great deal of interest, becoming one of the hottest topics in electrochemical energy storage (see Table S1 in the Supporting Information). [18,19] Regardless of the chemical nature of the electroactive species and the type of electrolytes, most RFBs rely on ion-selective membranes to separate the two redox electrolytes and to prevent the crossover of active compounds while allowing the migration of charge carriers. It is worth mentioning that membranes are not employed in some hybrid RFBs in which one of the active species is a solid, such as Zn, [20,21] Cd, [22] lithium, [23] or graphite.…”
mentioning
confidence: 99%
“…[4,5] Despite these advantages, high system prices (> $500kWh À1 in 2014) [6,7] have severely limited the commercial deployment of RFBs. [6,10] Although not commercially viable yet, NAqRFBs promise an umber of advantages over aqueous systems, including broader electrochemical windows (3-4 V), [1,11,12] which could enable higherc ell energy densities and aid in the implementation of multi-electrontransfer materials. [8,9] Recent techno-economic analyses predicted that both aqueous and nonaqueous( NAq) RFBs couldr each this aggressive target by decreasing manufacturing costs, advancing materials performance, and improving cell architecture.…”
Section: Introductionmentioning
confidence: 99%
“…To facilitate integration of a4he nergy-storage system,t he United States Department of Energy( DOE) Office of Electricity Deliverya nd Energy Reliability set at arget price of $150 kWh À1 ,i ncluding costs for installation and power-conditioning equipment. [12] Additionally,awide range of NAq solvents and supportings alts are available, and rational functionalization of the active speciescan be used to tailor physicochemical and electrochemical properties, [13] providing multiple pathways for device optimization and price reduction. [6,10] Although not commercially viable yet, NAqRFBs promise an umber of advantages over aqueous systems, including broader electrochemical windows (3-4 V), [1,11,12] which could enable higherc ell energy densities and aid in the implementation of multi-electrontransfer materials.…”
Section: Introductionmentioning
confidence: 99%
“…18,30,31,38,39,43,49 This study explores how variations in RFB performance due to supporting electrolyte and membrane selection impacts system cost. We focus on aqueous electrolytes, as opposed to nonaqueous electrolytes, 12,50,51 due to the higher technology-readiness level of AqRFBs and, consequently, the larger amount of associated device information for grid-relevant operation. First, we identify governing physical parameters, namely the membrane ASR, electrolyte conductivity, electrolyte viscosity, and cell potential, which significantly impact RFB cost.…”
Section: A3884mentioning
confidence: 99%
“…Physically, ν 2 represents the ratio of chargetransfer and ion-conduction rates in the porous electrode. [12] θ is the dimensionless limiting current ( Equation 13), defined as the ratio between the exchange and limiting current densities (i l , A m −2 ). Physically, θ represents the ratio of charge-transfer and mass transfer rates in the porous electrode.…”
Section: Computing Cell Area Specific Resistancementioning
confidence: 99%