4.6 Article

Understanding and improving anode performance in an alkaline membrane electrolyzer using statistical design of experiments

Journal

ELECTROCHIMICA ACTA
Volume 409, Issue -, Pages -

Publisher

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.electacta.2022.140001

Keywords

Anion exchange membrane; Electrolyzer; Water electrolysis; Oxygen evolution; Anode

Funding

  1. U.S. Department of Energy, Office of Energy Efficiency & Renewable Energy H2@Scale program [DE-EE0008833]

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The behavior of the oxygen-evolving positive electrode in an Anion Exchange Membrane Water Electrolyzer (AEMEL) is complex and influenced by various factors. This study investigates the effects of catalyst loading, catalyst selection, porous transport layer (PTL) type, and conductive additive content on the performance of the oxygen evolution reaction (OER). Through a design of experiments (DoE) approach and statistical analysis, the influence of each factor is evaluated. The findings can guide the optimal design of the electrode and aid in making design choices and performing techno-economic analyses.
The behavior of the oxygen-evolving positive electrode (i.e. anode) in the anion exchange membrane water electrolyzer (AEMEL) is complex and influenced by several factors. Very few studies have been performed to understand oxygen evolution reaction (OER) behavior by optimizing the individual factors that influence performance. This study highlights the effects of catalyst loading, catalyst selection, porous transport layer (PTL) type and conductive additive content. The influence of each factor is elucidated through a design of experiments (DoE) approach with a full statistical analysis. Electrochemical data, alongside Pareto charts, parametric trends and their mutual interactions are discussed. This DoE approach is also helpful in making useful predictions and discovering new combinations to be tested. The end result was a high-performance AEMEL able to operate at a current density of 1.0 A/cm(2) at 1.80 V with IrOx OER and PtNi hydrogen evolution reaction (HER) catalysts using 0.3 M KOH fed to the anode. Even lower operating voltage was observed with PbRuOx catalyst at the anode, 1.64 V @ 1.0 A/cm(2), though the cell decay rate was higher. Lastly, a IrOx/PtNi cell was stably operated continuously for 30 days (720 h) at 1.0 A/cm(2). This study can serve as a guide for optimal electrode design with insights into component-performance compromises, which can aid in making design choices and performing techno-economic analyses.

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