Journal
ELECTROCHIMICA ACTA
Volume 413, Issue -, Pages -Publisher
PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.electacta.2022.140078
Keywords
Anion exchange membrane water electrolysis; Critical raw materials free electrocatalysts; Supported NiMo alloy; Unsupported NiFe-oxide electrocatalyst; Hydrogen
Categories
Funding
- ANIONE project under the European Union's Horizon 2020 Research and Innovation Programme
- Fuel Cells and Hydrogen 2 Joint Undertaking (JU) [875024]
- European Union's Horizon 2020 Research and Innovation Programme
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A water electrolysis cell based on anion exchange membrane and critical raw materials-free electrocatalysts was developed, and suitable anode and cathode catalysts were investigated. The effect of recirculation of a diluted KOH solution was studied. The study found that high performance and suitable stability could be achieved under specific conditions.
A water electrolysis cell based on anion exchange membrane (AEM) and critical raw materials-free (CRM-free) electrocatalysts was developed. A NiFe-oxide electrocatalyst was used at the anode whereas a series of metallic electrocatalysts were investigated for the cathode, such as Ni, NiCu, NiMo, NiMo/KB. These were compared to a benchmark Pt/C cathode. CRMs-free anode and cathode catalysts were synthetized with a crystallite size of about 10 nm. The effect of recirculation through the cell of a diluted KOH solution was investigated. A concentration of 0.5-1 M KOH appeared necessary to achieve suitable performance at high current density. amongst the CRM-free cathodes, the NiMo/KB catalyst showed the best performance in the AEM electrolysis cell achieving a current density of 1 A cm(-2) at about 1.7-1.8 V/cell when it was used in combination with a NiFe-oxide anode and a 50 mu m thick Fumatech FAA-3-50 (R) hydrocarbon membrane. Durability tests showed an initial decrease of cell voltage with time during 2000 h operation at 1 A cm(-2) until reaching a steady state performance with an energy efficiency close to 80%. An increase of reversible losses during start-up and shutdown cycles was observed. Appropriate stability was observed during cycled operation between 0.2 and 1 A cm(-2); however, the voltage efficiency was slightly lower than in steady-state operation due to the occurrence of reversible losses during the cycles. Post operation analysis of electrocatalysts allowed getting a better comprehension of the phenomena occurring during the 2000 h durability test.
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