22–25 May 2023
Europe/London timezone

A mixed-wet pore network model for electrolyte imbibition in gas diffusion electrodes

25 May 2023, 10:45
1h 30m
Poster Presentation (MS09) Pore-scale modelling Poster

Speaker

Thorben Mager (Institute for Chemical Process Engineering, University of Stuttgart)

Description

Knowledge of electrolyte distribution inside Gas Diffusion Electrodes (GDE) is a key feature to improve the electrochemical behaviour of these electrodes. In processes like the chlor-alkali-electrolysis, a porous silver electrocatalyst is brought in contact with the liquid electrolyte and the gaseous reactants at the so-called three-phase boundary. To prevent flooding and to alter the wettability of the electrodes, non-wetting polytetrafluoroethylene is added in the manufacturing process. As shown by experimental work [1], the PTFE content has a high impact of the PTFE content on the electrode performance.

Based on FIB/SEM images of the silver electrodes, Direct Numerical Simulations (DNS) inside the pore system have been carried out using Smoothed Particle Hydrodynamics (SPH). This allows us to track the interface movement in a mixed-wettable porous electrode. Fig. 1 shows snapshots of the simulated filling process of a pore system. Hydrophobicity of the electrode significantly changes with consideration of the contact angle due to the electrowetting-effect [2], which had also be seen in experimentally for this GDE [3].

The DNS is computationally too expensive to model larger parts of the electrode while pore network models are computationally far less demanding. Therefore we combined pore network modelling and rigorous hydrodynamic simulations. First, a skeleton from pore space was extracted from the FIB/SEM-images. Then the skeleton is segmented into different parts of the pore systems. Second, characteristic properties like pore diameter and PTFE-Fraction that covers the pore wall are extracted along the connecting paths.

In a mixed-wet system, the entry pressure does not only depend on geometry and averaged wettability, but as well on the locally resolved wettability degree. In contrast to conventional pore network models, the highest entry pressure can be not determined by the narrowest nor the widest part of the pore system, but on the most hydrophobic one. This can be found by DNS or by more simplified models. Using this data as input, the electrolyte imbibition can be modelled by pore network models on representative electrode volumes.

References

References:
[1] D. Franzen et al., “Influence of binder content in silver-based gas diffusion electrodes on pore system and electrochemical performance,” J. Appl. Electrochem., vol. 49, no. 7, pp. 705–713, Jul. 2019.
[2] F. Mugele and J.-C. Baret, “Electrowetting: from basics to applications,” J. Phys. Condens. Matter, vol. 17, no. 28, pp. R705–R774, Jul. 2005.
[3] F. Bienen et al., “Investigating the electrowetting of silver‐based gas‐diffusion electrodes during oxygen reduction reaction with electrochemical and optical methods,” Electrochem. Sci. Adv., p. e2100158, Mar. 2022.

Participation In-Person
Country Germany
Energy Transition Focused Abstracts This abstract is related to Energy Transition
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Primary author

Thorben Mager (Institute for Chemical Process Engineering, University of Stuttgart)

Co-author

Prof. Ulrich Nieken (Institute of Chemical Process Engineering, University of Stuttgart)

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