2018
DOI: 10.1149/2.0471803jes
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Modeling of Oxygen Diffusion Resistance in Polymer Electrolyte Fuel Cells in the Intermediate Potential Region

Abstract: Oxygen transport resistance in the cathode catalyst layer of polymer electrolyte fuel cells is discussed. The performance of the cell is first calculated using a 1-dimensional through-plane model in which the activation overpotential and the diffusion-limited current density are fitted to experimental results. Potential-dependent transport resistance is then introduced to bridge the gap between the model prediction and the experimental result in the intermediate potential region. The potential dependent resist… Show more

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Cited by 16 publications
(14 citation statements)
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“…The limiting current is the maximum attainable current as the oxygen concentration on the surface of catalyst particles is depleted to zero, and it was used here to compare the mass transport ability of cathodes with various PTFE contents. [ 25 ] The total oxygen transport resistance is defined as the change of oxygen concentration divided by the average molar flux of oxygen, [ 23 ] and can be calculated from the cell limiting current based on Faraday's law and Fick's lawRnormalT=ΔCNnormalO2NO2=DO2effnormaldCnormalO2dδNO2=normali4Fwhere Δ C is the change of oxygen concentration, NO2 is the molar flux of oxygen, and DO2eff is the effective diffusion coefficient of oxygen. F and δ represent the Faraday constant and oxygen transport length, respectively.…”
Section: Methodsmentioning
confidence: 99%
“…The limiting current is the maximum attainable current as the oxygen concentration on the surface of catalyst particles is depleted to zero, and it was used here to compare the mass transport ability of cathodes with various PTFE contents. [ 25 ] The total oxygen transport resistance is defined as the change of oxygen concentration divided by the average molar flux of oxygen, [ 23 ] and can be calculated from the cell limiting current based on Faraday's law and Fick's lawRnormalT=ΔCNnormalO2NO2=DO2effnormaldCnormalO2dδNO2=normali4Fwhere Δ C is the change of oxygen concentration, NO2 is the molar flux of oxygen, and DO2eff is the effective diffusion coefficient of oxygen. F and δ represent the Faraday constant and oxygen transport length, respectively.…”
Section: Methodsmentioning
confidence: 99%
“…While the voltage of the Pt/C catalyst layer sharply attenuates in the high-current-density region, the CO ads Pt/C catalyst layer can maintain a certain power density even though the voltage decreases, especially at RH 20%. It is also found that with the reduction in RH, the proton conductivity and oxygen permeability of the ionomer decrease due to the decreased hydrophilic area at a lower water activity. ,, The sulfonic groups of the ionomer tend to bind more closely to the surface of Pt at lower humidity, worsening the oxygen transportation. , Therefore, the effect of ionomer distribution on oxygen transport resistance is more obvious at a lower RH.…”
Section: Resultsmentioning
confidence: 99%
“…More importantly, the performance of Pt/C-[MTBD][C 4 F 9 SO 3 ] in the high current density region was greatly improved, which is believed to be associated with facilitated oxygen transport within the electrode. In general, the oxygen transport resistance in the electrode mainly consists of the molecular diffusion resistance in the pores and the transport resistance at the interface between the ionomer and Pt [38][39][40][41]. It is likely that IL reduced the oxygen transport resistance by homogenously distributing the ionomer in the electrode [42,43] or increasing the oxygen permeability at the interface of Pt and ionomer [40].…”
Section: Resultsmentioning
confidence: 99%
“…In addition, the hydrophobic IL may limit the product water build up that hinders the mass transport of O 2 [10]. The experimental measurements of O 2 transport resistance using an internally established method [38,39] are ongoing to explore the mechanism. the mass transport of O2 [10].…”
Section: Resultsmentioning
confidence: 99%
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