Enhanced NiFe<sub>2</sub>O<sub>4</sub> Catalyst Performance and Stability in Anion Exchange Membrane Water Electrolysis: Influence of Iron Content and Membrane Selection

Anion exchange membrane (AEM) water electrolysis is a potentially inexpensive and efficient source of hydrogen production as it uses effective low-cost catalysts. The catalytic activity and performance of nickel iron oxide (NiFeO<sub>x</sub>) catalysts for hydrogen production in AEM wate...

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Bibliographic Details
Main Authors: Khaja Wahab Ahmed, Aidan Dobson, Saeed Habibpour, Michael Fowler
Format: Article
Language:English
Published: MDPI AG 2025-08-01
Series:Molecules
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Online Access:https://www.mdpi.com/1420-3049/30/15/3228
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Summary:Anion exchange membrane (AEM) water electrolysis is a potentially inexpensive and efficient source of hydrogen production as it uses effective low-cost catalysts. The catalytic activity and performance of nickel iron oxide (NiFeO<sub>x</sub>) catalysts for hydrogen production in AEM water electrolyzers were investigated. The NiFeO<sub>x</sub> catalysts were synthesized with various iron content weight percentages, and at the stoichiometric ratio for nickel ferrite (NiFe<sub>2</sub>O<sub>4</sub>). The catalytic activity of NiFeO<sub>x</sub> catalyst was evaluated by linear sweep voltammetry (LSV) and chronoamperometry for the oxygen evolution reaction (OER). NiFe<sub>2</sub>O<sub>4</sub> showed the highest activity for the OER in a three-electrode system, with 320 mA cm<sup>−2</sup> at 2 V in 1 M KOH solution. NiFe<sub>2</sub>O<sub>4</sub> displayed strong stability over a 600 h period at 50 mA cm<sup>−2</sup> in a three-electrode setup, with a degradation rate of 15 μV/h. In single-cell electrolysis using a X-37 T membrane, at 2.2 V in 1 M KOH, the NiFe<sub>2</sub>O<sub>4</sub> catalyst had the highest activity of 1100 mA cm<sup>−2</sup> at 45 °C, which increased with the temperature to 1503 mA cm<sup>−2</sup> at 55 °C. The performance of various membranes was examined, and the highest performance of the tested membranes was determined to be that of the Fumatech FAA-3-50 and FAS-50 membranes, implying that membrane performance is strongly correlated with membrane conductivity. The obtained Nyquist plots and equivalent circuit analysis were used to determine cell resistances. It was found that ohmic resistance decreases with an increase in temperature from 45 °C to 55 °C, implying the positive effect of temperature on AEM electrolysis. The FAA-3-50 and FAS-50 membranes were determined to have lower activation and ohmic resistances, indicative of higher conductivity and faster membrane charge transfer. NiFe<sub>2</sub>O<sub>4</sub> in an AEM water electrolyzer displayed strong stability, with a voltage degradation rate of 0.833 mV/h over the 12 h durability test.
ISSN:1420-3049