Cu/MnOx-CeO2 and Ni/MnOx-CeO2 catalysts for the water-gas shift reaction: Metal-support interaction

Monometallic copper and nickel catalysts supported on cerium-manganese mixed oxides are prepared, characterized and evaluated for the Water-Gas Shift (WGS) reaction. Active metal loading of 2.5 wt% and 7.5 wt% are used to impregnate MnOx-CeO2 supports with 30% and 50% Mn:Ce molar ratio. The structur...

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Autores principales: Poggio-Fraccari, E., Sambeth, J., Baronetti, G., Mariño, F.
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Acceso en línea:http://hdl.handle.net/20.500.12110/paper_03603199_v39_n16_p8675_PoggioFraccari
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spelling todo:paper_03603199_v39_n16_p8675_PoggioFraccari2023-10-03T15:26:28Z Cu/MnOx-CeO2 and Ni/MnOx-CeO2 catalysts for the water-gas shift reaction: Metal-support interaction Poggio-Fraccari, E. Sambeth, J. Baronetti, G. Mariño, F. Cerium Fuel cells Hydrogen purification Ilmenite Manganese Spinel Catalysts Cerium Fuel cells Ilmenite Manganese Manganese oxide Metals Water gas shift Catalytic behavior Copper and nickel catalysts Hydrogen purification Ilmenite structure Metal-support interactions Spinel Water-gas shift reaction (WGS) Water-gas-shift reactions Loading Monometallic copper and nickel catalysts supported on cerium-manganese mixed oxides are prepared, characterized and evaluated for the Water-Gas Shift (WGS) reaction. Active metal loading of 2.5 wt% and 7.5 wt% are used to impregnate MnOx-CeO2 supports with 30% and 50% Mn:Ce molar ratio. The structure of the samples strongly depends on both the active metal employed and the manganese content in the mixed support. For both Cu and Ni samples, the best catalytic behavior is found in samples supported on the MnOx-CeO2 oxides with 30% Mn:Ce molar ratio, as a result of the presence of CuxMnyO4 spinel-type phases in the case of copper catalysts and the presence of a NiMnO3 mixed oxide with defect ilmenite structure in the case of nickel catalysts. © 2014, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved. JOUR info:eu-repo/semantics/openAccess http://creativecommons.org/licenses/by/2.5/ar http://hdl.handle.net/20.500.12110/paper_03603199_v39_n16_p8675_PoggioFraccari
institution Universidad de Buenos Aires
institution_str I-28
repository_str R-134
collection Biblioteca Digital - Facultad de Ciencias Exactas y Naturales (UBA)
topic Cerium
Fuel cells
Hydrogen purification
Ilmenite
Manganese
Spinel
Catalysts
Cerium
Fuel cells
Ilmenite
Manganese
Manganese oxide
Metals
Water gas shift
Catalytic behavior
Copper and nickel catalysts
Hydrogen purification
Ilmenite structure
Metal-support interactions
Spinel
Water-gas shift reaction (WGS)
Water-gas-shift reactions
Loading
spellingShingle Cerium
Fuel cells
Hydrogen purification
Ilmenite
Manganese
Spinel
Catalysts
Cerium
Fuel cells
Ilmenite
Manganese
Manganese oxide
Metals
Water gas shift
Catalytic behavior
Copper and nickel catalysts
Hydrogen purification
Ilmenite structure
Metal-support interactions
Spinel
Water-gas shift reaction (WGS)
Water-gas-shift reactions
Loading
Poggio-Fraccari, E.
Sambeth, J.
Baronetti, G.
Mariño, F.
Cu/MnOx-CeO2 and Ni/MnOx-CeO2 catalysts for the water-gas shift reaction: Metal-support interaction
topic_facet Cerium
Fuel cells
Hydrogen purification
Ilmenite
Manganese
Spinel
Catalysts
Cerium
Fuel cells
Ilmenite
Manganese
Manganese oxide
Metals
Water gas shift
Catalytic behavior
Copper and nickel catalysts
Hydrogen purification
Ilmenite structure
Metal-support interactions
Spinel
Water-gas shift reaction (WGS)
Water-gas-shift reactions
Loading
description Monometallic copper and nickel catalysts supported on cerium-manganese mixed oxides are prepared, characterized and evaluated for the Water-Gas Shift (WGS) reaction. Active metal loading of 2.5 wt% and 7.5 wt% are used to impregnate MnOx-CeO2 supports with 30% and 50% Mn:Ce molar ratio. The structure of the samples strongly depends on both the active metal employed and the manganese content in the mixed support. For both Cu and Ni samples, the best catalytic behavior is found in samples supported on the MnOx-CeO2 oxides with 30% Mn:Ce molar ratio, as a result of the presence of CuxMnyO4 spinel-type phases in the case of copper catalysts and the presence of a NiMnO3 mixed oxide with defect ilmenite structure in the case of nickel catalysts. © 2014, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
format JOUR
author Poggio-Fraccari, E.
Sambeth, J.
Baronetti, G.
Mariño, F.
author_facet Poggio-Fraccari, E.
Sambeth, J.
Baronetti, G.
Mariño, F.
author_sort Poggio-Fraccari, E.
title Cu/MnOx-CeO2 and Ni/MnOx-CeO2 catalysts for the water-gas shift reaction: Metal-support interaction
title_short Cu/MnOx-CeO2 and Ni/MnOx-CeO2 catalysts for the water-gas shift reaction: Metal-support interaction
title_full Cu/MnOx-CeO2 and Ni/MnOx-CeO2 catalysts for the water-gas shift reaction: Metal-support interaction
title_fullStr Cu/MnOx-CeO2 and Ni/MnOx-CeO2 catalysts for the water-gas shift reaction: Metal-support interaction
title_full_unstemmed Cu/MnOx-CeO2 and Ni/MnOx-CeO2 catalysts for the water-gas shift reaction: Metal-support interaction
title_sort cu/mnox-ceo2 and ni/mnox-ceo2 catalysts for the water-gas shift reaction: metal-support interaction
url http://hdl.handle.net/20.500.12110/paper_03603199_v39_n16_p8675_PoggioFraccari
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AT baronettig cumnoxceo2andnimnoxceo2catalystsforthewatergasshiftreactionmetalsupportinteraction
AT marinof cumnoxceo2andnimnoxceo2catalystsforthewatergasshiftreactionmetalsupportinteraction
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