Imaging local pH in boundary layers at 3D electrodes in electrochemical flow systems

• Fluorescence lifetime imaging can map local pH gradients at 9 μm/2 Hz resolution. • Boundary layers around a 3D electrode surface develop in roughly 1 min (Fo = 0.1) • Current density defines the surface pH, while flow rate defines the affected range. • Local pH and voltages reveal that capacitive discharge can drive Faradaic reactions. • The charging potential tunes the ratio in kinetically- or diffusion-limited regimes. Electrochemical reactors, such as water electrolyzers, CO 2 electrolyzers, fuel cells, and flow batteries, will be essential in electrifying industry as part of the global transition towards a defossilized and sustainable economy. These technologies require further optimization to enhance efficiency and reduce costs for widespread adoption. Hydrodynamics and mass transfer at electrode–electrolyte interfaces significantly affect electrochemical conversion reactions by influencing the reactant availability and pH in the local reaction environment. 3D electrodes, such as flow-through foams and suspension electrodes, hold a great advantage over 2D electrodes as they moderate pH changes and reactant depletion by spreading the current over a larger electrode area and electrolyte volume. We study the diffusion boundary layer in operando around a single mm-sized particle, representing an element of a 3D electrode. We visualize the local and transient pH with Fluorescence Lifetime Imaging Microscopy (FLIM) during H 2 O reduction at various current densities and electrolyte flow velocities at a resolution down to 9 μm and 2 Hz. In addition, we apply an intermittent current to investigate how long the capacitive electric double layer of a suspension electrode particle can maintain an electrochemical reaction during their time of non-contact with a current collector, mimicking applications with Faradaic charge transfer ( i.e. flow batteries, microbial fuel cells, capacitance-based electrolyzers). We demonstrate that the diffusion boundary layer is not symmetrical, but depend on the direction of the electric field, the current density and the flow conditions. The substantial pH gradients and boundary layer formation at the scale of hundreds of micrometers underline the importance of controlling flow in or around electrodes, making 3D electrodes an important asset for creating suitable reaction conditions in mass transport-limited electrochemical conversions.

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Publication Details

Journal
Chemical Engineering Journal
Published
2025-02-16
DOI
https://doi.org/10.1016/j.cej.2025.160474
Citations
2
Primary Topic
Electrochemical Analysis and Applications
Type
article
Field-Weighted Citation Impact
1.03

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article

Imaging local pH in boundary layers at 3D electrodes in electrochemical flow systems

David A. Vermaas, Lorenz M. Baumgartner, Nathalie E. G. Ligthart, Julien Le Sommer et al.
2 citations
Chemical Engineering Journal
Electrochemical Analysis and Applications
1.03
article

Imaging local pH in boundary layers at 3D electrodes in electrochemical flow systems

David A. Vermaas, Lorenz M. Baumgartner, Nathalie E. G. Ligthart, Julien Le Sommer, Johan Tiemen Padding, Jorrit Bleeker
article en
2 citations

Abstract

• Fluorescence lifetime imaging can map local pH gradients at 9 μm/2 Hz resolution. • Boundary layers around a 3D electrode surface develop in roughly 1 min (Fo = 0.1) • Current density defines the surface pH, while flow rate defines the affected range. • Local pH and voltages reveal that capacitive discharge can drive Faradaic reactions. • The charging potential tunes the ratio in kinetically- or diffusion-limited regimes. Electrochemical reactors, such as water electrolyzers, CO 2 electrolyzers, fuel cells, and flow batteries, will be essential in electrifying industry as part of the global transition towards a defossilized and sustainable economy. These technologies require further optimization to enhance efficiency and reduce costs for widespread adoption. Hydrodynamics and mass transfer at electrode–electrolyte interfaces significantly affect electrochemical conversion reactions by influencing the reactant availability and pH in the local reaction environment. 3D electrodes, such as flow-through foams and suspension electrodes, hold a great advantage over 2D electrodes as they moderate pH changes and reactant depletion by spreading the current over a larger electrode area and electrolyte volume. We study the diffusion boundary layer in operando around a single mm-sized particle, representing an element of a 3D electrode. We visualize the local and transient pH with Fluorescence Lifetime Imaging Microscopy (FLIM) during H 2 O reduction at various current densities and electrolyte flow velocities at a resolution down to 9 μm and 2 Hz. In addition, we apply an intermittent current to investigate how long the capacitive electric double layer of a suspension electrode particle can maintain an electrochemical reaction during their time of non-contact with a current collector, mimicking applications with Faradaic charge transfer ( i.e. flow batteries, microbial fuel cells, capacitance-based electrolyzers). We demonstrate that the diffusion boundary layer is not symmetrical, but depend on the direction of the electric field, the current density and the flow conditions. The substantial pH gradients and boundary layer formation at the scale of hundreds of micrometers underline the importance of controlling flow in or around electrodes, making 3D electrodes an important asset for creating suitable reaction conditions in mass transport-limited electrochemical conversions.

Chemical Engineering JournalVol. 507
Delft University of Technology (NL)
H2020 European Research Council
Openalex Percentile: Top 31%
Electrochemical Analysis and Applications
1.03
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