2018
DOI: 10.1016/j.jpowsour.2017.12.014
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Validating and improving a zero-dimensional stack voltage model of the Vanadium Redox Flow Battery

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Cited by 42 publications
(38 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%
“…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%
“…32 To the best of our knowledge, no other original work has been published on pore-scale simulation of the RFB, while continuum-based modeling and optimization of the RFBs are still being actively pursued. [33][34][35][36] This gap in the modeling literature is partly attributed to the lack of a general pore-scale modeling framework with feasible computing requirements. Both the works of and Chen et al (2017) is based on direct numerical simulation (DNS), i.e.…”
mentioning
confidence: 99%
“…This hydraulic power loss consists the power consumption by two pumps and the pressure losses across the piping system, flow frame, and porous electrodes. In this case, study, we consider the same cell/stack/electrode design (with the same active electrode area) as in [21] and adopt the value of the scaling factor k = 1.41 from [21]. Table 3 shows the parameters, which are considered for the hydraulic system and the Figure 5 presents the pressure-drop (∆p) and total power consumption (P pump ) by the electrical pumps of VRB.…”
Section: Resultsmentioning
confidence: 99%
“…However, the determination of this actual surface area of the porous electrode can be difficult. Therefore, in this paper, we adopt a scaling factor (k) to represent the effect of the actual electrochemical surface area of the porous electrodes, as in [21]. Considering this actual electrode surface area, the current density of the VRB system can be calculated as follows:…”
Section: Vrb Stack Voltagementioning
confidence: 99%
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