2015
DOI: 10.1016/j.jpowsour.2014.10.055
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Assessing the performance of reactant transport layers and flow fields towards oxygen transport: A new imaging method based on chemiluminescence

Abstract: 30.04.15 KB. Ok to add published ao pape

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Cited by 8 publications
(70 citation statements)
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“…The geometry used for the simulations follows the one reported for the experimental apparatus [6], and is presented in Figure 1: a single-channel serpentine geometry was used for the flow field; a porous layer for the diffusion media, representing the macroporous carbon paper substrate (MPS); and finally a silica gel based catalytic layer (CL), where the catalyst is assumed homogeneously distributed. The CL includes a surface that follows the middle of the flow channel projection, crossing the entire CL domain thickness, used for probing the model (Fig.…”
Section: Methodsmentioning
confidence: 99%
See 3 more Smart Citations
“…The geometry used for the simulations follows the one reported for the experimental apparatus [6], and is presented in Figure 1: a single-channel serpentine geometry was used for the flow field; a porous layer for the diffusion media, representing the macroporous carbon paper substrate (MPS); and finally a silica gel based catalytic layer (CL), where the catalyst is assumed homogeneously distributed. The CL includes a surface that follows the middle of the flow channel projection, crossing the entire CL domain thickness, used for probing the model (Fig.…”
Section: Methodsmentioning
confidence: 99%
“…The outlet was defined by a constant pressure, with suppression of backflow, the value of it being supplied by the authors of reference [6]. To allow comparison with different systems, the Reynolds number was calculated using Q, the average kinematic viscosity over the entire flow channel domain, and the hydraulic diameter for rectangular channels, assuming the MPS as a solid wall.…”
Section: Methodsmentioning
confidence: 99%
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“…Notably,5 50 ccm O 2 was chosen because below 450 ccm the catalyst layer is not completely utilised due to an improper distribution of oxygen. [44] Anode and cathode operated at ag auge backpressure of approximately 210/210 kPa (H 2 and O 2 partial pressure at ca. 217 and 244 kPa abs taking into account water vapour) or 65/65 kPa (H 2 and O 2 partial pressure at ca.…”
Section: Membrane Electrode Assembly Preparationpefc Test Conditionsmentioning
confidence: 99%