“…The diffusion coefficient of Ce(IV) at a concentration of 0.1 mol dm -3 (see Table 1 [47]. Increasing the electrolyte flow rate to 17 cm s -1 had little effect on reducing the potential drop, as implied by its low " $ .…”
Section: Cyclic Voltammetry and Rotating Disc Experimentsmentioning
The conversion of soluble cerium redox species in the zinc-cerium redox flow battery and other electrochemical processes can be carried out at planar and porous platinised titanium electrodes.The active area, current density, mass transfer coefficient and linear electrolyte flow velocity through these structures have a direct influence on the reaction yield and the relationship between cell potential and operational current density during charge and discharge of a flow battery. A quantitative and practical characterization of the reaction environment at these electrodes is required. The volumetric mass transfer coefficient, " $ has been calculated from limiting current measurements for Ce(IV) ion reduction in a laboratory, rectangular channel flow cell. This factor can be used to predict fractional conversion and required electrode dimensions. Highly porous platinised titanium felt shows superior " $ values and is wellsuited as a high performance electrode material.
“…The diffusion coefficient of Ce(IV) at a concentration of 0.1 mol dm -3 (see Table 1 [47]. Increasing the electrolyte flow rate to 17 cm s -1 had little effect on reducing the potential drop, as implied by its low " $ .…”
Section: Cyclic Voltammetry and Rotating Disc Experimentsmentioning
The conversion of soluble cerium redox species in the zinc-cerium redox flow battery and other electrochemical processes can be carried out at planar and porous platinised titanium electrodes.The active area, current density, mass transfer coefficient and linear electrolyte flow velocity through these structures have a direct influence on the reaction yield and the relationship between cell potential and operational current density during charge and discharge of a flow battery. A quantitative and practical characterization of the reaction environment at these electrodes is required. The volumetric mass transfer coefficient, " $ has been calculated from limiting current measurements for Ce(IV) ion reduction in a laboratory, rectangular channel flow cell. This factor can be used to predict fractional conversion and required electrode dimensions. Highly porous platinised titanium felt shows superior " $ values and is wellsuited as a high performance electrode material.
“…Previous work [30,31] has shown that using charge and discharge current densities lower than 25 mA cm −2 at a temperature of 60°C led to a sharp fall in the coulombic efficiency of the zinc deposition/dissolution process, from ~96% down to ~81% for a 10 min charge (charge/discharge current density = 10 mA cm −2 ). The conventional Hull cell, with no flow, was thus used to explore if this fall was caused by the different nature of zinc deposits formed at these different densities.…”
Section: Resultsmentioning
confidence: 99%
“…Further investigation of this system was conducted by Plurion Ltd., the University of Southampton [27,28,29] and the University of Strathclyde [30,31,32,33]. Its great advantage is its power to weight ratio due to its high open circuit cell voltage (E cell = 2.4 V).…”
Section: Page 3 Of 25mentioning
confidence: 99%
“…Previous studies on the Zn-Ce flow cell have reported charge efficiencies of more than 90 % and energy efficiencies above 60 % at 10 mA cm −2 for over 100 cycles [30]. The material of choice there for the negative electrode was a polyvinyl ester or polyvinylidene fluoride-carbon composite material (BMA5) while a platinized titanium mesh was used as [29].…”
“…, with a redox potential of 1.15 V vs. Ag/AgCl/3.5 M KCl and which has been widely studied as positive electrolyte in redox flow batteries [24][25][26] was selected as the electroactive species in order to build asymmetric hybrid capacitors that use an activated carbon (AC) in the negative electrode and multiwalled carbon nanotubes (MWCNTs) or a modified graphite felt (GF) in the positive one.…”
The energy density of carbon based supercapacitors (CBSCs) was significantly increased by the addition of an inorganic redox species [Ce 2 (SO 4 ) 3 ] to an aqueous electrolyte (H 2 SO 4 ). The development of the faradaic processes on the positive electrode not only significantly increased the capacitance but also the operational cell voltage of these devices (up to 1.5 V) due to the high redox potentials at which the Ce 3+ /Ce 4+ reactions occur. Therefore, in asymmetric CBSCs assembled using an activated carbon as negative electrode and MWCNTs as the positive one, the addition of Ce 2 (SO 4 ) 3 moderately increases the energy density of the device (from 1.24 W h kg -1 to 5.08 W h kg -1 ). When a modified graphite felt is used as positive electrode the energy density of the cell reaches values as high as 13.84 W h kg -1 . The resultant systems become asymmetric hybrid devices where energy is stored due to double layer formation in the negative electrode and the development of the faradaic process in the positive electrode, which acts as a battery-type electrode.
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