2012
DOI: 10.1016/j.jpowsour.2012.07.037
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Quantitative analysis of carbon corrosion during fuel cell start-up and shut-down by anode purging

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Cited by 64 publications
(39 citation statements)
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“…This may be because degradation depends on the residence time of the gas front which passes through the cell and thus on the specific test protocol for start up and shut down. 65 A detailed discussion of degradation phenomena in start/ stop procedures can be found here. 13 …”
Section: F154mentioning
confidence: 99%
“…This may be because degradation depends on the residence time of the gas front which passes through the cell and thus on the specific test protocol for start up and shut down. 65 A detailed discussion of degradation phenomena in start/ stop procedures can be found here. 13 …”
Section: F154mentioning
confidence: 99%
“…However, in terms of durability, this material exhibits important disadvantages related to its poor electrochemical and chemical resistance in the aggressive operational conditions of the HT‐PEMFC. These harsh conditions are given due to the polibenzimidazole (PBI) based membranes (typical membranes used in HT‐PEMFC) must be doped with phosphoric acid in order to get acceptable protonic condition, and this acid, combined with the high temperature operational range, performs a strong degradation on the Vulcan carbon based electrode components . Furthermore, the electrochemical carbon corrosion starts to appear at potentials over 0.267 V vs RHE, resulting in a several corrosion at voltages over 1.2 V. These voltage values are easily achieved during the turn‐on and shut‐down processes during the fuel cell operation, and also in open circuit voltage (OCV) conditions ,.…”
Section: Introductionmentioning
confidence: 99%
“…These harsh conditions are given due to the polibenzimidazole (PBI) based membranes (typical membranes used in HT‐PEMFC) must be doped with phosphoric acid in order to get acceptable protonic condition, and this acid, combined with the high temperature operational range, performs a strong degradation on the Vulcan carbon based electrode components . Furthermore, the electrochemical carbon corrosion starts to appear at potentials over 0.267 V vs RHE, resulting in a several corrosion at voltages over 1.2 V. These voltage values are easily achieved during the turn‐on and shut‐down processes during the fuel cell operation, and also in open circuit voltage (OCV) conditions ,. The degradation of the Vulcan carbon carries out some problems related with the performance and durability of the fuel cell (mass transfer limitation, migration and agglomeration of the platinum particles, or the increasing of the ohmic resistance of the electrodes, due to the degradation of the carbonaceous structure of the electrode).…”
Section: Introductionmentioning
confidence: 99%
“…However during the start-up and shut-down operation, the cathode can reach potentials higher than 1V (5,6). Therefore, carbon BPPs are prone to corrosion in fuel cells for automotive applications.…”
Section: Introductionmentioning
confidence: 99%