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Liquid phase pentanoic acid hydrogenation in decane as a solvent (180 oC, hydrogen pressure 25 bar) was studied over monometallic Ir and bimetallic Ir-Re catalysts supported on alumina, ceria and zirconia, as well as carbon support Sibunit. Before catalytic test all catalysts were preliminary treated in Н2 at 415 oC during 5 h. An XPS study revealed predominant metallic state for Ir in studied catalysts while Re was partially oxidized. Conversion of pentanoic acid changed in the row Ir/CeO2 < Ir/ZrO2 < IrRe/ZrO2 < IrRe/Al2O3 ~ IrRe/C. Selectivity to pentanol was elevated over bimetallic catalysts in the sequence Ir/Al2O3 < Ir/CeO2 ~ Ir/ZrO2 < IrRe/ZrO2 < IrRe/Al2O3 ~ IrRe/C. It was shown that doping of Ir with Re gives a rise of pentanoic acid conversion and selectivity to pentanol in the absence of byside decarboxylation reaction. A series of the most active catalyst IrRe/Al2O3 was prepared varying Ir particle size from 0.8 to 1.7 nm as verified by TEM. Both pentanoic acid conversion and selectivity to pentanol over IrRe/Al2O3 catalyst increased with an increase of mean Ir particle size.

Hydrogenation of Pentanoic Acid into Pentanol Over Ir and Ir-Re Catalysts: Effect of Support and Ir Dispersion