A deeper understanding of flooding dynamics in gas diffusion electrodes for CO2 electrolyzer: how interfacial pressure shapes gas–liquid stability

Gas-fed CO 2 electrolyzers are a promising technology for sustainable fuel and chemical production, but their industrial deployment is limited by the instability of gas diffusion electrodes (GDEs), particularly in microfluidic flow cells (MFCs). A key failure mechanism is electrode flooding, which discontinues CO 2 transport and favours hydrogen evolution. Although pressure control across the gas–liquid interface has emerged as a strategy to mitigate flooding, the precise role of differential pressure (ΔP) between gas and liquid side of the GDE remains poorly understood and inconsistently defined in literature. In this work, we systematically explore how gas and liquid pressure management alters the GDE interface, focusing on the understudied “ flow-by ” regime. Using Cu nanoparticles as a model catalyst and operating at industrially relevant current densities (0.5 A cm −2 ), we monitor flooding dynamics through real-time pressure readings, product selectivity analysis, electrochemical impedance spectroscopy (EIS) and field emission scanning electron microscopy (FE-SEM) in different electrochemical setups with several commercial Gas Diffusion Layers (GDL). Our results demonstrate that a ΔP of 30 mbar can fully suppress flooding, preserving catalyst performance and enabling selective CO 2 reduction for over 6 h at 0.5 A cm −2 , almost an order-of-magnitude improvement over uncontrolled system. The experimental ΔP value is confirmed by multiphysics simulations, by modelling capillary-driven liquid invasion and gas transport, in which a predicted onset value of 20 mbar is defined as the required value to prevent the flooding. This work provides the first integrated framework combining pressure tuning, diagnostics, and multi-physics simulation to define and optimize flow-by operation, offering actionable insights for designing robust, high-performance CO 2 electrolyzers. • Integration of multiphysics simulations with high-current experiments • Pressure-driven suppression of flooding • Generalizable methodology for GDE evaluation

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Publication Details

Journal
Chemical Engineering Journal
Published
2025-12-05
DOI
https://doi.org/10.1016/j.cej.2025.171393
Citations
1
Primary Topic
CO2 Reduction Techniques and Catalysts
Type
article
Field-Weighted Citation Impact
0.36
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article

A deeper understanding of flooding dynamics in gas diffusion electrodes for CO2 electrolyzer: how interfacial pressure shapes gas–liquid stability

Marco Etzi, Alessio Mezza, Candido Fabrizio Pirri, Laura Gatti et al.
1 citations
Chemical Engineering Journal
CO2 Reduction Techniques and Catalysts
0.36
article

A deeper understanding of flooding dynamics in gas diffusion electrodes for CO2 electrolyzer: how interfacial pressure shapes gas–liquid stability

Marco Etzi, Alessio Mezza, Candido Fabrizio Pirri, Laura Gatti, Adriano Sacco, Matteo Alberghini, Alessio Tommasi, Daniele Sassone, Santiago Quesada
article en
1 citations

Abstract

Gas-fed CO 2 electrolyzers are a promising technology for sustainable fuel and chemical production, but their industrial deployment is limited by the instability of gas diffusion electrodes (GDEs), particularly in microfluidic flow cells (MFCs). A key failure mechanism is electrode flooding, which discontinues CO 2 transport and favours hydrogen evolution. Although pressure control across the gas–liquid interface has emerged as a strategy to mitigate flooding, the precise role of differential pressure (ΔP) between gas and liquid side of the GDE remains poorly understood and inconsistently defined in literature. In this work, we systematically explore how gas and liquid pressure management alters the GDE interface, focusing on the understudied “ flow-by ” regime. Using Cu nanoparticles as a model catalyst and operating at industrially relevant current densities (0.5 A cm −2 ), we monitor flooding dynamics through real-time pressure readings, product selectivity analysis, electrochemical impedance spectroscopy (EIS) and field emission scanning electron microscopy (FE-SEM) in different electrochemical setups with several commercial Gas Diffusion Layers (GDL). Our results demonstrate that a ΔP of 30 mbar can fully suppress flooding, preserving catalyst performance and enabling selective CO 2 reduction for over 6 h at 0.5 A cm −2 , almost an order-of-magnitude improvement over uncontrolled system. The experimental ΔP value is confirmed by multiphysics simulations, by modelling capillary-driven liquid invasion and gas transport, in which a predicted onset value of 20 mbar is defined as the required value to prevent the flooding. This work provides the first integrated framework combining pressure tuning, diagnostics, and multi-physics simulation to define and optimize flow-by operation, offering actionable insights for designing robust, high-performance CO 2 electrolyzers. • Integration of multiphysics simulations with high-current experiments • Pressure-driven suppression of flooding • Generalizable methodology for GDE evaluation

Chemical Engineering JournalVol. 527
Politecnico di Torino (IT), Italian Institute of Technology (IT), DIAD (Italy) (IT), Center for Sustainable Future Technologies (IT)
Openalex Percentile: Top 35%
CO2 Reduction Techniques and Catalysts
0.36
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