Antonio Monzón
www.mendeley.com
0000-0002-7836-5777
Universidad de Zaragoza
99 papers found
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Deactivation by sintering of Ni/TiOj and Ni/TiCh-AhOj sol-gel hydrogénation catalysts
Acetylene hydrogenation with a modified Ni-Zn-Al catalyst. Influence of the operating conditions on the coking rate
Deactivation of Ni supported on alumina-titania: Modelling of coke deposition in the phenylacetylene hydrogenation
Deactivation by sintering of Ni/TiO2 and Ni/TiO2-Al2O3 sol-gel hydrogenation catalysts
Acetylene hydrogenation on Ni–Al–Cr oxide catalysts: the role of added Zn
Hydrogenation of 1,3-butadiene on Pd/SiO2 in the presence of H2S deactivation and reactivation of the catalyst
Effect of Zn Content on Catalytic Activity and Physicochemical Properties of Ni-Based Catalysts for Selective Hydrogenation of Acetylene
Deactivation by coking and poisoning of spinel-type Ni catalysts
Modelling of sulfur deactivation of naphtha-reforming catalysts Structure sensitivity in cyclopentane hydrogenolysis
Deactivation by sintering and coking of Sol-Gel NiO-Al2O3-TiO2 hydrogenation catalysts
Activity, selectivity and coking of bimetallic Ni-Co-spinel catalysts in selective hydrogenation reactions
Dehydrogenation of isopropylic alcohol on a Cu/SiO2 catalyst: a study of the activity evolution and reactivation of the catalyst
Effect of thermal aging upon the regeneration kinetics of a coked Cr2O3Al2O3 catalyst
Coking Kinetics of a Cr2O3/Al2O3 Catalyst during 1-Butene Dehydrogenation: Effect of H2 Partial Pressure
Regeneration of Fixed-Bed Catalytic Reactors Deactivated by Coke: Influence of Operating Conditions and of Different Pretreatments of the Coke Deposits
Oxidation of Methane to Synthesis Gas in a Fluidized Bed Reactor Using MgO-Based Catalysts
Modelling of sintering kinetics of naphtha-reforming Pt/Al2O3-Cl catalysts
Hydrogenation of acetylene over Ni/NiAl2O4 catalyst: Characterization, coking, and reaction studies
Fourier transform infrared spectroscopic study of coke deposits on a Cr2O3Al2O3 catalyst
Kinetic modelling of the deactivation of a commercial silica—alumina catalyst during isopropylbenzene cracking
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