2020
DOI: 10.1016/j.enconman.2020.113046
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Combined effects of flow channel configuration and operating conditions on PEM fuel cell performance

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Cited by 55 publications
(19 citation statements)
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“…The membrane water content at equilibrium is usually related to the local water activity via algebraic expression, for which examples are reported in Table 9 and illustrated in Figure 4, showing that a good agreement is found for undersaturated states (a < 1), whereas different values are reported for over-saturated conditions (a > 1). The membrane water content is experimentally determined as a function of the local relative humidity and of water activity a as in Equation (18), where p H 2 O represents the partial pressure of the water vapour. The relationship between the water concentration and water content λ is given by Equation ( 17), with ρ m,dry the dry membrane density and EW m the membrane equivalent weight (represented by the dry mass of the membrane (ionomer) over the number of moles of SO 3 -) which takes a value of 1100 kg/kmol (for Nafion 112, 115 and 117) or 2100 kg/kmol (for Nafion 211 and 212) [5].…”
Section: Diffusive Modelmentioning
confidence: 99%
See 1 more Smart Citation
“…The membrane water content at equilibrium is usually related to the local water activity via algebraic expression, for which examples are reported in Table 9 and illustrated in Figure 4, showing that a good agreement is found for undersaturated states (a < 1), whereas different values are reported for over-saturated conditions (a > 1). The membrane water content is experimentally determined as a function of the local relative humidity and of water activity a as in Equation (18), where p H 2 O represents the partial pressure of the water vapour. The relationship between the water concentration and water content λ is given by Equation ( 17), with ρ m,dry the dry membrane density and EW m the membrane equivalent weight (represented by the dry mass of the membrane (ionomer) over the number of moles of SO 3 -) which takes a value of 1100 kg/kmol (for Nafion 112, 115 and 117) or 2100 kg/kmol (for Nafion 211 and 212) [5].…”
Section: Diffusive Modelmentioning
confidence: 99%
“…Another example is the choice between straightparallel and serpentine gas distributors [16], with the former excelling in reduced pressure losses for reactants delivery while the latter optimising water removal. Such designs are motivated by water handling issues; therefore, they testify the relevance of an accurate modelling of water management if 3D-CFD simulations are to be used alongside testing for design guidance of future PEMFC power systems [17][18][19].…”
mentioning
confidence: 99%
“…To avoid local reactants’ starvation and improve the reactants’ utilization, the transverse mass transfer should be enhanced. [ 20 ] Several studies reported that the secondary flow and convection in through‐plane direction can improve the mass transfer of reactants between the channel and the diffusion layer. Min et al [ 21 ] performed a numerical analysis of the secondary flow of modified serpentine channels, and the results indicate that increasing segment number or the channel path number in a segment can strengthen the secondary flow and improve the cell performance.…”
Section: Introductionmentioning
confidence: 99%
“…Second, for narrowing the straight channel in flow fields, two methods can be used [12][13][14][15][16]. One is to increase the baffles in the flow channel as Figure 2b,c.…”
Section: Introductionmentioning
confidence: 99%