2020
DOI: 10.3390/en13246556
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Generic Dynamical Model of PEM Electrolyser under Intermittent Sources

Abstract: Proton Exchange Membrane (PEM) water electrolysis system is one of the promising technologies to produce green hydrogen from renewable energy sources (wind and solar). However, performance and dynamic analysis of PEM water electrolysis systems are challenging due to the intermittent nature of such sources and involved multi-physical behaviour of the components and subsystems. This study proposes a generic dynamical model of the PEM electrolysis system represented in a modular fashion using Bond Graph (BG) as a… Show more

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Cited by 26 publications
(8 citation statements)
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“…When operating PEM water electrolysis at a low current density, the main contributors to overpotential losses are sources other than mass transport overpotential. Mass transfer overpotential performance influence is often insignificant under these conditions [110].…”
Section: Impact Of Bubbles On Mass Transport Overpotentialmentioning
confidence: 99%
“…When operating PEM water electrolysis at a low current density, the main contributors to overpotential losses are sources other than mass transport overpotential. Mass transfer overpotential performance influence is often insignificant under these conditions [110].…”
Section: Impact Of Bubbles On Mass Transport Overpotentialmentioning
confidence: 99%
“…At the cathode side, the hydrogen protons recombine with the hydrogen electrons in pairs to form hydrogen (H 2 ) gas [33,34]. The technologies used for water electrolysis can be classified into three main categories: Alkaline (ALK) electrolysers, Polymer Electrolyte Membrane (PEM) electrolysers, and Solid-Oxide Electrolysis Cells (SOECs).…”
Section: Green Hydrogen Productionmentioning
confidence: 99%
“…While their electrochemical behavior has been extensively studied, their dynamic thermal behavior has been mostly simplified. A large number of models use the so-called lumped parameter approach, where incoming and outgoing heat fluxes are calculated based on the assumption that the electrolysis stack has a uniform temperature at each time step (Crespi et al 2023;Espinosa-López et al 2018;García-Valverde, Espinosa and Urbina 2012;Sood et al 2020). This type of model has already been implemented in Modelica by Webster and Bode (2019).…”
Section: Introductionmentioning
confidence: 99%