Influence of mixing time on a reversal tolerant anode measured ex situ for a PEMFC

Journal Article (2024)
Author(s)

S. J.T. Homan (cellcentric GmbH & Co. KG, TU Delft - ChemE/Catalysis Engineering)

K. Aylar (cellcentric GmbH & Co. KG)

A. Jurjevic (cellcentric GmbH & Co. KG)

M. Scolari (cellcentric GmbH & Co. KG)

A. Urakawa (TU Delft - ChemE/Catalysis Engineering)

P. Taheri (TU Delft - Team Peyman Taheri)

Research Group
ChemE/Catalysis Engineering
DOI related publication
https://doi.org/10.1016/j.ijhydene.2024.01.236
More Info
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Publication Year
2024
Language
English
Research Group
ChemE/Catalysis Engineering
Volume number
59
Pages (from-to)
1166-1173
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Abstract

When no hydrogen can reach the Pt catalyst in the anode for the hydrogen oxidation reaction (HOR) of an operating proton exchange membrane fuel cell (PEMFC), the anode potential increases and causes the cell potential to be reversed compared to normal operation conditions. During this reversal, the oxygen evolution reaction (OER) and carbon oxidation reaction (COR) will occur at the anode, where the COR has devastating consequences for the electrode. Introducing an OER catalyst limits the COR to occur, which makes a reversal tolerant anode (RTA). In this research, RTAs are differentiated by applying different ball milling times during catalyst layer processing, forming big and small OER (IrOx/TiOx) and HOR (Pt/C) catalyst particles. The two different particle sizes were electrochemically tested using a rotating disc electrode (RDE). Both catalyst sizes show a decrease in OER activity (mA cm−2) accompanied by loss of the ionomer in a self-developed accelerated stress test (AST). The small particle RTAs show higher OER activity as a result of increased surface area. However, during a chronopotentiometry measurement, which mimics a fuel cell reversal, the small particle coatings show a worse reversal tolerance. This phenomenon can be attributed to the increased difficulty in removing oxygen bubbles.

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