Mitigating Electrolyte Flooding for Electrochemical CO2Reduction via Infiltration of Hydrophobic Particles in a Gas Diffusion Layer

Journal Article (2022)
Author(s)

Yuming Wu (University of Queensland)

Liam Charlesworth (University of Queensland)

Irving Maglaya (University of Queensland)

Mohamed Nazmi Idros (University of Queensland)

Mengran Li (TU Delft - ChemE/Materials for Energy Conversion and Storage)

Tom Burdyny (TU Delft - ChemE/Materials for Energy Conversion and Storage)

Geoff G.X. Wang (University of Queensland)

Thomas E. Rufford (University of Queensland)

Research Group
ChemE/Materials for Energy Conversion and Storage
Copyright
© 2022 Yuming Wu, Liam Charlesworth, Irving Maglaya, Mohamed Nazmi Idros, Mengran Li, T.E. Burdyny, Geoff Wang, Thomas E. Rufford
DOI related publication
https://doi.org/10.1021/acsenergylett.2c01555
More Info
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Publication Year
2022
Language
English
Copyright
© 2022 Yuming Wu, Liam Charlesworth, Irving Maglaya, Mohamed Nazmi Idros, Mengran Li, T.E. Burdyny, Geoff Wang, Thomas E. Rufford
Research Group
ChemE/Materials for Energy Conversion and Storage
Issue number
9
Volume number
7
Pages (from-to)
2884-2892
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Abstract

Achieving operational stability at high current densities remains a challenge in CO2 electrolyzers due to flooding of the gas diffusion layer (GDL) that supports the electrocatalyst. We mitigated electrode flooding at high current densities using a vacuum-assisted infiltration method to embed 200-400 nm-sized polytetrafluoroethylene (PTFE) particles at the interface of the microporous layer (MPL) and carbon cloth in a commercial GDL. In CO2 electrolysis to CO over a silver nanoparticle catalyst on the GDL, the PTFE-embedded GDL not only just exhibited less than 10% of the electrolyte seepage rates observed in untreated GDLs at a current density of 300 mA·cm-2 but also expanded the electrochemical active area across the testing conditions. The PTFE-embedded GDL also maintained a Faradaic efficiency for CO2 electrolysis to CO above 80% for more than 100 h at 100 mA·cm-2, which was a 50-fold improvement in the stable operation time of the electrolyzer.

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