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Abstract

<title>Abstract</title> <p> The Co <sub>3</sub> O <sub>4</sub> -based catalyst was prepared by precipitation method, followed by lanthanum incorporation through incipient wetness impregnation. All catalysts were evaluated in the preferential oxidation (PROX) of carbon monoxide in hydrogen-rich streams. Catalysts characterised was performed using XRD, TEM, SEM, FTIR, TGA, TPR and XPS. The XRD and FTIR results confirmed the formation of the spinel CO <sub>3</sub> O <sub>4</sub> phase. The TPR measurements confirmed the formation of La-O-Co linkage, evidencing strong electronic and structural interaction between La species and Co <sub>3</sub> O <sub>4</sub> lattice. This was further confirmed by XPS, which showed an increased concentration of oxygen vacancies and a concomitant decrease in surface hydroxyl groups. This change is associated with a reduction in the fraction of Co <sup>3+</sup> relative to Co <sup>2+</sup> upon the incorporation of La species to Co <sub>3</sub> O <sub>4</sub> . As a result, an improvement in PROX performance was observed for the 1wt.% La/Co <sub>3</sub> O <sub>4</sub> catalyst, which exhibited optimum activity at relatively lower temperatures (~ 60 to 120 <sup>o</sup> C). A slight decrease in CO conversion with time on stream was observed for 1wt.% La/Co <sub>3</sub> O <sub>4</sub> in the presence of moisture, attributable to La doping, which suppresses OH-vacancy-assisted dissociative adsorption of H <sub>2</sub> O. Furthermore, the introduction of CO <sub>2</sub> into the feed resulted in an approximately 30% decrease in catalytic activity with time on stream. Overall, La doped Co <sub>3</sub> O <sub>4</sub> appears as a promising catalyst for low temperature (~ 80–120 <sup>o</sup> C) CO reduction in hydrogen rich streams, aligning with requirements for efficient proton exchange membrane fuel cells. </p>

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Keywords

catalyst confirmed which decrease incorporation

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