2020
DOI: 10.1002/ese3.765
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Nonisothermal two‐phase modeling of the effect of linear nonuniform catalyst layer on polymer electrolyte membrane fuel cell performance

Abstract: This is an open access article under the terms of the Creative Commons Attribution License, which permits use, distribution and reproduction in any medium, provided the original work is properly cited.

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Cited by 9 publications
(5 citation statements)
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References 43 publications
(101 reference statements)
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“…The cell characteristic was better at the low operating voltage when more catalysts were placed under the flow channel, near the membrane side and at the inlet of CH, but the uneven distribution of catalyst loading had little effect on cell performance at high operating voltage. Sabzpoushan et al 16 studied two kinds of linear distributions of catalyst loading along the gas flow direction, including linearly decreasing and linearly increasing distributions. The polarization curves and species distributions for cases of uniform distribution and two linear distributions were compared.…”
Section: Establishedmentioning
confidence: 99%
“…The cell characteristic was better at the low operating voltage when more catalysts were placed under the flow channel, near the membrane side and at the inlet of CH, but the uneven distribution of catalyst loading had little effect on cell performance at high operating voltage. Sabzpoushan et al 16 studied two kinds of linear distributions of catalyst loading along the gas flow direction, including linearly decreasing and linearly increasing distributions. The polarization curves and species distributions for cases of uniform distribution and two linear distributions were compared.…”
Section: Establishedmentioning
confidence: 99%
“…Global greenhouse gas (GHG) emissions must, however, decline by 50% by 2030 and reach net zero by the middle of the century if the worst effects of climate change are to be avoided [13]. Therefore, it is imperative to develop more effective technologies to avoid these toxic gases [14][15][16][17]. Our usage of clean technologies must expand by at least one order of magnitude if we are to decarbonize our energy supply and achieve its net zero goals [18].…”
Section: Introductionmentioning
confidence: 99%
“…From the steady-state models, the numerical works are oriented towards the entire fuel cell flow fields and experimental validation, as seen in Carcadea et al [43]. Another interesting approach related to steady-state models is seen in Sabzpoushan et al [44] where the authors have conducted a numerical study, using a two-dimensional steady-state model, to investigate the influence of non-uniform catalyst loading using a constant slope along the channel, where the performance of the cell is increased by 1.6% in power density and 5% in voltage. The transient approach is also gaining traction and oriented towards studying temporally resolved mass concentrations of the gas constituents with and without purge strategies in Peng et al [45].…”
Section: Introductionmentioning
confidence: 99%
“…Transient models are also developed to study the influence of the inlet velocity fluctuations on the performance of the cell, Kulikovsky [46], as well as performance of the cell with the existence of catalyst layer cracks under relative humidity cycling conditions, Qin et al [47]. Some of the mentioned approaches [43][44][45][46][47] will be the focus of the following works due to increasing the computational complexity, which is not feasible at the moment due to the prolonged time required since optimization must be conducted in a reasonable amount of time.…”
Section: Introductionmentioning
confidence: 99%