Copper and nickel catalysts supported on praseodymium-doped ceria (PDC) for the water-gas shift reaction

The aim of this work is to study the behavior of Cu and Ni catalysts supported on praseodymium-doped ceria (PDC) for the WGS reaction. Samples were prepared by impregnation of several PDC supports (praseodymium content in the range 0-50 wt%) synthesized by the urea thermal decomposition method. Bare...

Descripción completa

Guardado en:

Detalles Bibliográficos
Autores principales:	Poggio-Fraccari, E., Mariño, F., Laborde, M., Baronetti, G.
Formato:	JOUR
Materias:	Ceria support CO removal Cu-Ni catalysts Hydrogen Praseodymium Copper and nickel catalysts Fixed bed reactor Oxygen storage capacity Praseodymium-doped ceria Thermal decomposition methods Water-gas shift reaction (WGS) Chemical reactors Copper Decomposition Loading Nickel Oxygen Urea Water gas shift Catalyst supports
Acceso en línea:	http://hdl.handle.net/20.500.12110/paper_0926860X_v460-461_n_p15_PoggioFraccari
Aporte de:	Biblioteca Digital - Facultad de Ciencias Exactas y Naturales (UBA) de Universidad de Buenos Aires

Ejemplares similares

Copper and nickel catalysts supported on praseodymium-doped ceria (PDC) for the water-gas shift reaction
Publicado: (2013)

Cu and/or Ni catalysts over CePr oxide for the water gas shift reaction: an experimental study, kinetic fitting and reactor simulation
por: Poggio-Fraccari, E., et al.

Cu and/or Ni catalysts over CePr oxide for the water gas shift reaction: an experimental study, kinetic fitting and reactor simulation
Publicado: (2017)

Ce-Mn mixed oxides as supports of copper- and nickel-based catalysts for water-gas shift reaction
por: Poggio Fraccari, E., et al.

Ce-Mn mixed oxides as supports of copper- and nickel-based catalysts for water-gas shift reaction
Publicado: (2014)

Cu/MnOx-CeO2 and Ni/MnOx-CeO2 catalysts for the water-gas shift reaction: Metal-support interaction
por: Poggio-Fraccari, E., et al.

Zr promotion effect in CO 2 methanation over ceria supported nickel catalysts
Publicado: (2019)

Zr promotion effect in CO 2 methanation over ceria supported nickel catalysts
por: Iglesias, I., et al.

Cu/MnOx-CeO2 and Ni/MnOx-CeO2 catalysts for the water-gas shift reaction: Metal-support interaction
Publicado: (2014)

Low-Cost Catalysts for the Water Gas Shift Reaction Based on Cu–Ni on La-Promoted Ceria
por: Poggio-Fraccari, E., et al.

Low-Cost Catalysts for the Water Gas Shift Reaction Based on Cu–Ni on La-Promoted Ceria
Publicado: (2018)

Supported base metal catalysts for the preferential oxidation of carbon monoxide in the presence of excess hydrogen (PROX)
Publicado: (2005)

Supported base metal catalysts for the preferential oxidation of carbon monoxide in the presence of excess hydrogen (PROX)
por: Mariño, F., et al.

Pr3+ surface fraction in CePr mixed oxides determined by XPS analysis
por: Poggio-Fraccari, E., et al.

Preferential oxidation of carbon monoxide in the presence of hydrogen (PROX) over noble metals and transition metal oxides: Advantages and drawbacks
Publicado: (2008)

Preferential oxidation of carbon monoxide in the presence of hydrogen (PROX) over noble metals and transition metal oxides: Advantages and drawbacks
por: Bion, N., et al.

Hydrogen from steam reforming of ethanol. characterization and performance of copper-nickel supported catalysts
por: Duhalde, Stella Maris, et al.
Publicado: (1998)

Hydrogen from steam reforming of ethanol. characterization and performance of copper-nickel supported catalysts
por: Mariño, F.J., et al.

Pr3+ surface fraction in CePr mixed oxides determined by XPS analysis
Publicado: (2018)

Production of hydrogen by catalytic steam reforming of oxygenated model compounds on Ni-modified supported catalysts. Simulation and experimental study
Publicado: (2015)

Production of hydrogen by catalytic steam reforming of oxygenated model compounds on Ni-modified supported catalysts. Simulation and experimental study
por: González-Gil, R., et al.

Effect of temperature and reduction on the activity of high temperature water gas shift catalysts
Publicado: (1986)

Effect of temperature and reduction on the activity of high temperature water gas shift catalysts
por: Gonzalez, J.C., et al.

Influence of the calcination temperature on the structure and reducibility of nanoceria obtained from crystalline Ce(OH)CO3 precursor
por: Jobbagy, Matias
Publicado: (2011)

Influence of the calcination temperature on the structure and reducibility of nanoceria obtained from crystalline Ce(OH)CO3 precursor
por: Poggio, E., et al.

Simulation of a low temperature water gas shift reactor using the heterogeneous model/application to a pem fuel cell
Publicado: (2006)

Simulation of a low temperature water gas shift reactor using the heterogeneous model/application to a pem fuel cell
por: Giunta, P., et al.

Bio-ethanol steam reforming on Ni/Al2O3 catalyst
Publicado: (2004)

Bio-ethanol steam reforming on Ni/Al2O3 catalyst
por: Comas, J., et al.

Hydrogen production from steam reforming of bioethanol using Cu/Ni/K/γ-Al2O3 catalysts. Effect of Ni
Publicado: (2001)

Hydrogen production from steam reforming of bioethanol using Cu/Ni/K/γ-Al2O3 catalysts. Effect of Ni
por: Mariño, F., et al.

Cu-Ni-K/γ-Al2O3 supported catalysts for ethanol steam reforming: Formation of hydrotalcite-type compounds as a result of metal-support interaction
por: Jobbagy, Matias
Publicado: (2002)

Cu-Ni-K/γ-Al2O3 supported catalysts for ethanol steam reforming: Formation of hydrotalcite-type compounds as a result of metal-support interaction
por: Mariño, F., et al.

Effect of intraparticle diffusion on catalyst decay
por: Amadeo, Norma Elvira
Publicado: (1996)

Effect of intraparticle diffusion on catalyst decay
por: Chocrón, M., et al.

Removal of nitrate from drinking water by using PdCu structured catalysts based on cordierite monoliths
por: Jaworski, María Angélica, et al.
Publicado: (2019)

Hydrogen production by glycerol steam reforming: How Mg doping affects the catalytic behaviour of Ni/Al2O3 catalysts
Publicado: (2016)

Hydrogen production by glycerol steam reforming: How Mg doping affects the catalytic behaviour of Ni/Al2O3 catalysts
por: Dieuzeide, M.L., et al.

Steam reforming of glycerol over Ni/Mg/γ-Al 2O 3 catalysts. Effect of calcination temperatures
Publicado: (2012)

Steam reforming of glycerol over Ni/Mg/γ-Al 2O 3 catalysts. Effect of calcination temperatures
por: Dieuzeide, M.L., et al.