2009
DOI: 10.1016/j.electacta.2009.04.073
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Modelling and simulations of carbon corrosion during operation of a Polymer Electrolyte Membrane fuel cell

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Cited by 55 publications
(30 citation statements)
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“…In addition to measuring or mathematically predicting the high cathode potential experienced during the startup and shutdown processes, researchers have also conducted other related tests, such as measuring the current distribution in segmented cells [60][61][62], monitoring the concentration of CO or CO 2 during startup and shutdown [59,63], evaluating the effect of cell design (flow field structure and GDL thickness) on start-stop phenomena [64,65], and conducting modeling studies [58,[66][67][68][69][70][71][72][73] on water management and carbon-corrosion during startup and shutdown. All the test results have confirmed performance degradation during the startup and shutdown processes of PEMFCs.…”
Section: Reverse Currentmentioning
confidence: 99%
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“…In addition to measuring or mathematically predicting the high cathode potential experienced during the startup and shutdown processes, researchers have also conducted other related tests, such as measuring the current distribution in segmented cells [60][61][62], monitoring the concentration of CO or CO 2 during startup and shutdown [59,63], evaluating the effect of cell design (flow field structure and GDL thickness) on start-stop phenomena [64,65], and conducting modeling studies [58,[66][67][68][69][70][71][72][73] on water management and carbon-corrosion during startup and shutdown. All the test results have confirmed performance degradation during the startup and shutdown processes of PEMFCs.…”
Section: Reverse Currentmentioning
confidence: 99%
“…In 2008, Ofstad [74] reported creating a transient hydrogen/air interface in the anode layer. In Jingwei's modeling study [73], the results indicated that the rate of carbon corrosion at the cathode side of the fuel starvation region was strongly dependent on oxygen diffusion through the membrane. The concentration gradient across the membrane is the driving force for oxygen to permeate from the cathode to the anode, according to Fick's first law.…”
Section: Fuel Starvationmentioning
confidence: 99%
“…Moreover, the flows supplied to the anode and the cathode should exceed the hydrogen/oxygen flows necessary for reaction, W H 2,React and W O 2,React . The hydrogen flow W H 2,React and the oxygen flow W O 2,React that react to produce a certain cell current I are defined by (11) and (12), respectively [20].…”
Section: Methodsmentioning
confidence: 99%
“…The adsorbed CO blocks active platinum sites at the anode, leading to the inhibition of reactions and to performance losses. These losses can decrease performance significantly with increasing adsorption of CO [10], [11]. The CO reaction is expressed in (15).…”
Section: B Carbon Monoxide (Co) Poisoningmentioning
confidence: 99%
“…These two hydrogen-deficient conditions are similar but the damage to the fuel cell is completely different, and in fact heterogeneous fuel distribution cannot cause cell reversal but current reversal [24]. Local fuel starvation, or partial hydrogen coverage, damages the air electrode and induces oxygen migration across the membrane from the cathode [25,26]. There are two mathematical guides to help us distinguish between and get a clear picture of these two situations by demonstrating electron diffusion and gas flow.…”
Section: Pemfc Anodementioning
confidence: 99%