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Definition of Critical Metrics for Performance Evaluation and Multiphase Flow Modeling in an Alkaline Electrolyzer Using CFD

Author

Listed:
  • Marco Dreoni

    (Department of Industrial Engineering, Università degli Studi di Firenze, Via di Santa Marta 3, 50139 Firenze, Italy)

  • Francesco Balduzzi

    (Department of Industrial Engineering, Università degli Studi di Firenze, Via di Santa Marta 3, 50139 Firenze, Italy)

  • Syed Sahil Hossain

    (McPhy Energy Deutschland GmbH, Schwartzkopffstraße 1, 15745 Wildau, Germany)

  • Matthias Neben

    (McPhy Energy Deutschland GmbH, Schwartzkopffstraße 1, 15745 Wildau, Germany)

  • Francesco Maria Ferro

    (McPhy Energy Italia Srl, Via Ayrton Senna 22, 56028 San Miniato, Italy)

  • Giovanni Ferrara

    (Department of Industrial Engineering, Università degli Studi di Firenze, Via di Santa Marta 3, 50139 Firenze, Italy)

  • Alessandro Bianchini

    (Department of Industrial Engineering, Università degli Studi di Firenze, Via di Santa Marta 3, 50139 Firenze, Italy)

Abstract

Gas evolution and flow patterns inside an alkaline electrolyzer cell strongly affect efficiency, although such effects have not been explored in detail to date. The present study aims to critically analyze the dependence of cell performance on the multiphase flow phenomena, defining some key metrics for its assessment using CFD. Six performance indicators, involving gas accumulation, bubble coverage, and flow uniformity, are applied to a 3D CFD model of an alkaline cathodic cell, and possible optimizations of the cell geometry are evaluated. The results demonstrate the complexity of defining the optimal indicator, which strictly depends on the case study and on the analysis at hand. For the cell analyzed herein, the parameters linked to the electrode volume fraction were indicated as the most influential on the cell efficiency, allowing us to define the best geometry case during the optimization. Furthermore, a sensitivity analysis was conducted, which showed that higher mass flow rates are generally preferable as they are linked to higher bubble removal. Higher current densities, allowing enhanced gas production, are instead associated with slightly lower efficiencies and stronger nonuniformity of the electrolyte flow inside the cell.

Suggested Citation

  • Marco Dreoni & Francesco Balduzzi & Syed Sahil Hossain & Matthias Neben & Francesco Maria Ferro & Giovanni Ferrara & Alessandro Bianchini, 2024. "Definition of Critical Metrics for Performance Evaluation and Multiphase Flow Modeling in an Alkaline Electrolyzer Using CFD," Energies, MDPI, vol. 17(21), pages 1-18, October.
  • Handle: RePEc:gam:jeners:v:17:y:2024:i:21:p:5317-:d:1506683
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    References listed on IDEAS

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    1. Alam, Afroz & Park, Chungi & Lee, Jaeseung & Ju, Hyunchul, 2020. "Comparative analysis of performance of alkaline water electrolyzer by using porous separator and ion-solvating polybenzimidazole membrane," Renewable Energy, Elsevier, vol. 166(C), pages 222-233.
    2. Longchang Xue & Shuaishuai Song & Wei Chen & Bin Liu & Xin Wang, 2024. "Enhancing Efficiency in Alkaline Electrolysis Cells: Optimizing Flow Channels through Multiphase Computational Fluid Dynamics Modeling," Energies, MDPI, vol. 17(2), pages 1-18, January.
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