2018
DOI: 10.1016/j.apenergy.2018.06.148
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Analysis of flow field design on vanadium redox flow battery performance: Development of 3D computational fluid dynamic model and experimental validation

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Cited by 161 publications
(115 citation statements)
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“…Messaggi et al published a computational fluid dynamics (CFD) model of a 25 cm 2 half‐cell incorporating mass and charge transfer and reaction kinetics . They demonstrated agreement with experimental polarization curves and showed a heterogeneous distribution of reaction rates with maxima over the ribs between neighboring channels far away from the turns connecting channel passes.…”
Section: Introductionmentioning
confidence: 91%
“…Messaggi et al published a computational fluid dynamics (CFD) model of a 25 cm 2 half‐cell incorporating mass and charge transfer and reaction kinetics . They demonstrated agreement with experimental polarization curves and showed a heterogeneous distribution of reaction rates with maxima over the ribs between neighboring channels far away from the turns connecting channel passes.…”
Section: Introductionmentioning
confidence: 91%
“…Moreover, studies devoted to combined optimization of the flow field type and electrolyte flow rate are sometimes difficult to compare with each other and their conclusions diverge both on a quantitative as well as qualitative level . For example, in the works it was shown that power of MEA with interdigitated flow fields exceeds the same value for the serpentine flow field but in the work, on the contrary, cell with serpentine flow field demonstrated higher discharge power.…”
Section: Introductionmentioning
confidence: 99%
“…Electrolytes were supplied to the cell at a flow rate from 10 to 50 ml min −1 using 2‐channel peristatic pump (Longerpump, BT100‐1F). The initial charging process was performed in a potentiostatic mode (1.7 V) in two stages with an intermediate replacement of the electrolyte in the tank of the positive electrode . The potentiostatic charging continued until a cutoff current density of 3 mA cm −2 and 6 mA cm −2 was achieved for N117 and N211 membrane.…”
Section: Introductionmentioning
confidence: 99%
“…These simulations typically require measured, fitted, or referenced chemical property data in addition to specified governing equations and geometric dimensions for establishing the computational domain. Three-dimensional (3D) RFB models have been developed and compared to experimental results [14,[40][41][42][43][44][45][46][47]. However, given the various feature lengths in a RFB, 3D model are computationally expensive, which has, in turn, motivated the development of two-dimensional (2D) RFB models to more quickly compare simulation results with lab-scale cells [48][49][50][51][52][53][54][55][56][57].…”
Section: Introductionmentioning
confidence: 99%