Comparison of a commercial water-gas shift catalyst and La modified Cu-based catalysts prepared by deposition-precipitation in methanol steam reforming.

Turk J Chem · 2022 · PMC10395737 · PMID 37538757

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a decreasing trendno p-value reported

an increasing trendno p-value reported

An increasing trend in CO selectivity for catalysts with supports calcined at 750 °C and a decreasing trend for catalysts with supports calcined at 1000 °C were observed.

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