2011
DOI: 10.1016/j.jpowsour.2011.08.035
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Degradation of polymer electrolyte membrane fuel cells repetitively exposed to reverse current condition under different temperature

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Cited by 45 publications
(29 citation statements)
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“…[16] Whereby the t mem refers to the membrane thickness (15 or 18 μm) and the apparent activation energy for proton conduction (E act H + ) was taken as 6 kJ/mol. 22 The electrical bulk and contact resistances (η [18] Under the simplifying assumption that the OER in the electrolytic part of the cell can be neglected, an analytical expression for the polarization curve of the electrolytic cell could be obtained. However, in the case of using a cathode catalyst with a graphitized carbon support, the effective potential in the cathode of the electrolytic part of the cell increases to values at which the OER currents become substantial, so that this simplifying assumption is not anymore satisfied.…”
Section: Kinetic H 2 /Air Anode Susd Modelmentioning
confidence: 99%
See 1 more Smart Citation
“…[16] Whereby the t mem refers to the membrane thickness (15 or 18 μm) and the apparent activation energy for proton conduction (E act H + ) was taken as 6 kJ/mol. 22 The electrical bulk and contact resistances (η [18] Under the simplifying assumption that the OER in the electrolytic part of the cell can be neglected, an analytical expression for the polarization curve of the electrolytic cell could be obtained. However, in the case of using a cathode catalyst with a graphitized carbon support, the effective potential in the cathode of the electrolytic part of the cell increases to values at which the OER currents become substantial, so that this simplifying assumption is not anymore satisfied.…”
Section: Kinetic H 2 /Air Anode Susd Modelmentioning
confidence: 99%
“…16 Only in the studies by Kreitmeier et al 17 and by Jo et al 18 the temperature was varied while Figure 1. Schematic of a start-up and/or shut-down (SUSD) event in a PEMFC, sketching the passage of a H 2 /air anode front through the anode flow-field (H 2 -filled regions in red, air-filled regions in blue) while the cathode flow-field is filled with air.…”
mentioning
confidence: 99%
“…As shown in several operating parameters [33][34][35][36][37][38][39] that can have an impact on the degradation rate of PEMFCs under startup and shutdown cycles, including cathode humidity [37,38], cell temperature [33], application of a dummy load [35,36], and gas supply sequences [34]. The hydrogen/air interface during the startup and shutdown processes was mimicked by purging the anode and cathode channels with air after continuous air and hydrogen were supplied.…”
Section: Accelerated Lifetime Tests Under Startup-shutdown Cyclesmentioning
confidence: 99%
“…After the start/stop cycles, the relative number of particles with a diameter ≤2.5 nm declined from 57.20% in a fresh MEA to 1.92%. Cho et al combined the results of cross-sectional SEM and TEM to evaluate Pt/C degradation [33,34,36,38,39,45,59].…”
Section: Agglomeration And/or Dissolution Of Pt Particlesmentioning
confidence: 99%
“…Our previous studies [11e13] confirmed that the cathode degradation depended significantly on the relative humidity (RH) [11], cell temperature [12], and residual oxygen partial pressure in the gas channels [13]. With increasing RH, cell temperature, and oxygen partial pressure, the cell degradation was accelerated, likely due to an increase in the oxidation reaction rates of Eqs.…”
Section: Introductionmentioning
confidence: 77%