Development and validation of a quasi-2D electrolysis stack model with a focus on dynamic thermal behavior

Maintaining a constant stack temperature and minimizing temperature gradients within the stack during operation is critical to the efficiency and durability of proton exchange membrane (PEM) electrolyzers. At the same time, the significant amount of heat released during operation provides opportunities to reuse this heat, potentially improving economic efficiency and contributing to the decarbonization of the heating sector. The design of stack temperature and heat recovery control systems requires accurate and effective models that describe the dynamic thermal behavior of the stack during load changes without being overly computationally intensive. Therefore, this paper presents a dynamic quasi-2D model of a PEM electrolysis stack that rapidly calculates these dynamic processes in a generally applicable manner. The model also incorporates phenomena such as gas and liquid crossover and pressure drop. We validated the performance of the model with experimental data from a PEM electrolysis test bench and demonstrated its accuracy in describing the electrochemical and dynamic thermal behavior. The stack voltage was simulated with a mean absolute deviation (MAD) of 0.0895 V and the anode outlet temperature with an MAD of 0.127 K, while the simulated time constants of the thermal step responses showed an MAD of 4.06 %. • Novel dynamic PEM stack model with focus on thermal behavior is presented. • Model incorporates gas-liquid heat transfer and pressure drop phenomena. • Electrochemical and dynamic thermal behavior is validated with experimental data. • Validation shows higher gas fraction in cooling water increases heat transfer.

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Publication Details

Journal
International Journal of Hydrogen Energy
Published
2025-03-20
DOI
https://doi.org/10.1016/j.ijhydene.2025.03.225
Citations
4
Primary Topic
Fuel Cells and Related Materials
Type
article
Field-Weighted Citation Impact
2.92

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article

Development and validation of a quasi-2D electrolysis stack model with a focus on dynamic thermal behavior

Ansgar Reimann, Paul Kohlenbach, Lars Röntzsch, Clemens Schneider
4 citations
International Journal of Hydrogen Energy
Fuel Cells and Related Materials
2.92
article

Development and validation of a quasi-2D electrolysis stack model with a focus on dynamic thermal behavior

Ansgar Reimann, Paul Kohlenbach, Lars Röntzsch, Clemens Schneider
article en
4 citations

Abstract

Maintaining a constant stack temperature and minimizing temperature gradients within the stack during operation is critical to the efficiency and durability of proton exchange membrane (PEM) electrolyzers. At the same time, the significant amount of heat released during operation provides opportunities to reuse this heat, potentially improving economic efficiency and contributing to the decarbonization of the heating sector. The design of stack temperature and heat recovery control systems requires accurate and effective models that describe the dynamic thermal behavior of the stack during load changes without being overly computationally intensive. Therefore, this paper presents a dynamic quasi-2D model of a PEM electrolysis stack that rapidly calculates these dynamic processes in a generally applicable manner. The model also incorporates phenomena such as gas and liquid crossover and pressure drop. We validated the performance of the model with experimental data from a PEM electrolysis test bench and demonstrated its accuracy in describing the electrochemical and dynamic thermal behavior. The stack voltage was simulated with a mean absolute deviation (MAD) of 0.0895 V and the anode outlet temperature with an MAD of 0.127 K, while the simulated time constants of the thermal step responses showed an MAD of 4.06 %. • Novel dynamic PEM stack model with focus on thermal behavior is presented. • Model incorporates gas-liquid heat transfer and pressure drop phenomena. • Electrochemical and dynamic thermal behavior is validated with experimental data. • Validation shows higher gas fraction in cooling water increases heat transfer.

International Journal of Hydrogen EnergyVol. 118
Berliner Hochschule für Technik (DE), Fraunhofer Research Institution for Energy Infrastructures and Geotechnologies IEG (DE), Brandenburg University of Technology Cottbus-Senftenberg (DE)
Bundesministerium für Bildung und Forschung
Affordable and clean energy
Openalex Percentile: Top 10%
Fuel Cells and Related Materials
2.92
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