Applied Catalysis B: Environmental · 2025 · 10 citations · 72 references
EngineeringChemical EngineeringChemistryElectrochemical EngineeringElectrochemistryMachine LearningElectrochemical Cell DesignElectrochemical CellsElectrochemical Energy ConversionElectrochemical Energy StorageElectrode MaterialsFuel CellsCatalytic Energy ConversionEnergy Storage ApplicationsOxygen Evolution ReactionOxygen Reduction CatalystsOxygen Reduction ReactionPerovskite Electrode MaterialsPerovskite OxidesPhysicochemical Descriptors
Due to their high efficiency and versatility, solid oxide electrochemical cells (SOCs) are poised to play a significant role in future energy conversion and storage applications. In recent years, SOCs have bifurcated into two distinct categories: traditional oxygen-ion conducting SOCs that typically operate from ~650 850 °C and the more recent proton-conducting ceramic (PCC) SOCs that typically operate from ~400 650 °C. Current performance and lifetime of both oxygen-ion conducting SOCs and PCCs is primarily limited by the air/steam electrode, which facilitates the oxygen reduction reaction (ORR) during fuel cell operation and must also facilitate the oxygen evolution reaction (OER) during electrolysis operation. Here, we present a newly designed high-entropy double perovskite oxide suitable as a universal ORR/OER electrode for both oxygen-ion conducting SOCs and PCCs. Machine learning methods are applied to identify chemical descriptors for highly catalytic high-entropy double perovskite oxides (AA’B 2 O 6 ) across a large compositional space. Based on the machine-learning guidance, we ultimately converge on Ba 0.9 Cs 0.1 (Ca 0.2 Gd 0.2 La 0.2 Pr 0.2 Sr 0.2 )Co 1.5 Fe 0.5 O 6 (CsBaHEO) as a universal air/steam electrode. Structure stabilization is accomplished by an equimolar five-cation high-entropy composition on the A’-site, while cesium substitution on the A-site enhances the electrical conductivity and leads to a higher oxygen vacancy concentration. This material exhibits versatility and high performance in reversible oxygen-ion SOCs, reversible PCCs, and also large-scale tubular PCCs. For example, the CsBaHEO-based PCC reaches 1018 mW∙cm -2 at 600°C, while a large-scale tubular PCC using CsBaHEO for electrolysis achieves a hydrogen production rate of 21.314 ml∙min -1 at 600 °C.
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