2020
DOI: 10.1016/j.jpowsour.2020.227930
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Thermodynamically consistent reduced dimensionality electrochemical model for proton exchange membrane fuel cell performance modelling and control

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Cited by 34 publications
(42 citation statements)
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“…The model is a zero-dimensional physical PEMFC model, and Figure 1 gives a schematic overview. It utilizes, amongst others, mass balances, linear nozzle equations, diffusion equations, electrochemical equations, and the ideal gas law [22][23][24]. However, it does not consider energy balances and thus cannot model the FC temperature over time.…”
Section: Model Descriptionmentioning
confidence: 99%
“…The model is a zero-dimensional physical PEMFC model, and Figure 1 gives a schematic overview. It utilizes, amongst others, mass balances, linear nozzle equations, diffusion equations, electrochemical equations, and the ideal gas law [22][23][24]. However, it does not consider energy balances and thus cannot model the FC temperature over time.…”
Section: Model Descriptionmentioning
confidence: 99%
“…The electrochemical submodel, i.e., the dependence of the FC voltage V on the current I and internal states, is adopted from [33]. The power produced by the FC stack is defined as P st = V I.…”
Section: Power and Efficiencymentioning
confidence: 99%
“…This corresponds with to the fact that the time constants of the electrochemical reactions are several orders of magnitude faster then the time-constants associated with the convective and diffusive transport of species [29]. The electrochemical model is described and discussed in detail in [30]. Aggregating all differential equations describing the fuel cell stack leads to a highly non-linear state-space model of the formẋ…”
Section: Derivation Of Model Equationsmentioning
confidence: 99%