2015
DOI: 10.1016/j.jpowsour.2015.05.100
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Numerical investigation and thermodynamic analysis of the effect of electrolyte flow rate on performance of all vanadium redox flow batteries

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Cited by 54 publications
(36 citation statements)
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“…According to previous work [88,89], the exponent constant a is typically in the range of 0.3 to 0.5 for laminar flow. This value of a (i.e., 0.4) is also widely reported in previous modeling studies [14,30,38,[43][44][45][46][90][91][92][93][94][95]. For b, the fitted value, 1.33 × 10 −5 , is within the range of the previously reported values; for example, k m,− = 1.69 × 10 −5 |u| 0.4 and k m,+ = 1.07 × 10 −5 |u| 0.4 as reported in Delanghe et al [96].…”
Section: Model Parameterssupporting
confidence: 86%
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“…According to previous work [88,89], the exponent constant a is typically in the range of 0.3 to 0.5 for laminar flow. This value of a (i.e., 0.4) is also widely reported in previous modeling studies [14,30,38,[43][44][45][46][90][91][92][93][94][95]. For b, the fitted value, 1.33 × 10 −5 , is within the range of the previously reported values; for example, k m,− = 1.69 × 10 −5 |u| 0.4 and k m,+ = 1.07 × 10 −5 |u| 0.4 as reported in Delanghe et al [96].…”
Section: Model Parameterssupporting
confidence: 86%
“…Three-dimensional (3D) RFB models have been developed and compared to experimental results [14,[30][31][32][33][34][35][36]. 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 [37][38][39][40][41][42][43][44][45][46]. These 2D models are generally created by omitting the influence of one spatial dimension in the RFB, which can result in inaccurate cell-level fluid dynamic values [47].…”
Section: Introductionmentioning
confidence: 99%
“…According to previous work [88,89], the exponent constant a is typically in the range of 0.3 to 0.5 for laminar flow. This value of a (i.e., 0.4) is also widely reported in previous modeling studies [14,30,38,[43][44][45][46][90][91][92][93][94][95].…”
Section: Model Parameterssupporting
confidence: 85%
“…Pump power losses for different types of bends, valves, and tube diameters in the electrolyte circuit have been also considered . Pressure drop differences between the positive and negative half‐cells can be substantial, and the cell design should aim to reduce them. Finally, it has been shown that interdigitated felt electrodes could reduce pressure losses in vanadium RFB stacks to ca.…”
Section: Introductionmentioning
confidence: 99%