Perovskite as nickel catalyst precursor - impact on catalyst stability on xylose aqueous-phase hydrogenation

Precursors materials with formula, La 1− x Ce x Al 0.18 Ni 0.82 O 3 ( x = 0.0, 0.1, 0.5, 0.7), were successfully used as precursors to prepare Ni nanoclusters to be used as catalysts in the hydrogenation of xylose to xylitol. For the Ce free and lower Ce content ( x = 0.0; 0.1), the perovskite struc...

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Veröffentlicht in:RSC advances 2016-01, Vol.6 (72), p.67817-67826
Hauptverfasser: Morales, Ruddy, Campos, Cristian H, Fierro, J. L. G, Fraga, Marco A, Pecchi, Gina
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Campos, Cristian H
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Pecchi, Gina
description Precursors materials with formula, La 1− x Ce x Al 0.18 Ni 0.82 O 3 ( x = 0.0, 0.1, 0.5, 0.7), were successfully used as precursors to prepare Ni nanoclusters to be used as catalysts in the hydrogenation of xylose to xylitol. For the Ce free and lower Ce content ( x = 0.0; 0.1), the perovskite structure was obtained, whereas for a higher Ce content ( x = 0.5; 0.7), an ordinary CeO 2 -La 2 O 3 solid dissolution with no perovskite structure were obtained. Under the reduction conditions, the perovskite structure leads to ∼30% of metallic Ni without any loss of the perovskite structure ( x = 0.0; 0.1) and the CeO 2 -La 2 O 3 solid dissolution allows a Ni reduction of ∼40% of Ni ( x = 0.5; 0.7). As expected, the similar reduced Ni content does not show large differences in the aqueous-phase xylose hydrogenation product distribution, or large difference in the precursors. The perovskite structure ( x = 0.0; 0.1) and solid dissolution ( x = 0.5; 0.7) highlight the importance of the perovskite structure in the remarkable leaching resistance showed by the Ni perovskite-precursor ( x = 0.0; 0.1) catalysts, showing no Ni leaching over 6 h of reaction in an aqueous medium. Precursors materials with formula, La 1− x Ce x Al 0.18 Ni 0.82 O 3 ( x = 0.0, 0.1, 0.5, 0.7), were successfully used as precursors to prepare Ni nanoclusters to be used as catalysts in the hydrogenation of xylose to xylitol.
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Under the reduction conditions, the perovskite structure leads to ∼30% of metallic Ni without any loss of the perovskite structure ( x = 0.0; 0.1) and the CeO 2 -La 2 O 3 solid dissolution allows a Ni reduction of ∼40% of Ni ( x = 0.5; 0.7). As expected, the similar reduced Ni content does not show large differences in the aqueous-phase xylose hydrogenation product distribution, or large difference in the precursors. The perovskite structure ( x = 0.0; 0.1) and solid dissolution ( x = 0.5; 0.7) highlight the importance of the perovskite structure in the remarkable leaching resistance showed by the Ni perovskite-precursor ( x = 0.0; 0.1) catalysts, showing no Ni leaching over 6 h of reaction in an aqueous medium. Precursors materials with formula, La 1− x Ce x Al 0.18 Ni 0.82 O 3 ( x = 0.0, 0.1, 0.5, 0.7), were successfully used as precursors to prepare Ni nanoclusters to be used as catalysts in the hydrogenation of xylose to xylitol.</abstract><doi>10.1039/c6ra13395a</doi><tpages>1</tpages><orcidid>https://orcid.org/0000-0001-8592-5384</orcidid></addata></record>
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source Royal Society Of Chemistry Journals 2008-
subjects Catalysts
Dissolution
Hydrogenation
Leaching
Nickel
Perovskite structure
Precursors
Xylose
title Perovskite as nickel catalyst precursor - impact on catalyst stability on xylose aqueous-phase hydrogenation
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