Abstract

Backbone electrodes based on an electronic conductor and a protonic conductor show advantages for proton ceramic electrolyzer cells (PCECs). This work, aims to shed further light on the nature of the rate determining steps in the anode operation and improve the reaction rate in high steam pressure electrolysis mode by (i) adjusting their catalytic activity through electrode infiltration with catalytic electronic-conducting nanoparticles; and (ii) electrochemical activation of surface species by applying a net current through the electrode. A composite formed by La0.8Sr0.2MnO3−δ (LSM) and BaCe0.2Zr0.7Y0.1O3−δ (BCZY27) was deposited on proton-conducting BCZY27 electrolytes and studied in symmetrical cells to investigate the anode microstructure and electrochemical performance. Electrochemical impedance spectroscopy (EIS) measurements were performed in the 800–500 °C range under 3 bar of pressure of wet air (75% of steam). LSM/BCZY27 50/50 vol% showed the best performance with an electrode polarization resistance (Rp) of 6.04 Ω cm2 at 700 °C and high steam pressure (0.75 bar of air and 2.25 bar of steam) whereas LSM/BCZY27 60/40 vol% presented a Rp of 18.9 Ω cm2. The backbone electrodes were infiltrated using aqueous solutions of metal precursors to boost the electrocatalytic activity towards water splitting and oxygen evolution. The infiltrated cells were fired at 850 °C for 2 h to obtain the desired crystalline nanoparticles (Pr6O11, CeO2, ZrO2 and Pr6O11–CeO2) and electrochemically tested under high steam pressures and bias currents to investigate the influence of catalytic activation on surface exchange kinetics. Among the tested catalysts, the lowest electrode polarization resistances (<0.2 Ω cm2) were reached for the Pr6O11, CeO2 and Pr6O11–CeO2 catalysts at 700 °C by applying current densities ranging from 1.57 to 14.15 mA cm−2, and the Pr6O11–CeO2-activated LSM/BCZY27 electrode exhibited the best performance. Finally, the effect of pO2 and pH2O was investigated aiming to characterize the rate limiting processes in the electrodes.

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