Industrial & Engineering Chemistry Research · 2008 · 83 citations · 12 references
Natural SciencesChemical EngineeringChemistryCatalysisChemical KineticsOrganic ChemistryCatalytic MechanismsCatalytic Reaction KineticsChemical Kinetics ModelingChemical Reaction KineticsKinetic ModelingReaction Mechanism ModelingCatalytic Reaction MechanismsCompetitive AdsorptionCompetitive Adsorption KineticsHydrogenationHydrogenation CatalysisHydrogenation ReactionsLangmuir-hinshelwood KineticsLangmuir-hinshelwood Mechanism
Hydrogenation of six model feeds containing three-, two-, and one-ring aromatic compounds was investigated to gain insights into the aromatic hydrogenation reaction chemistry over a commercial NiMo catalyst under practical reaction conditions. The hydrogenation reactivity of the aromatic compounds followed the following order: phenanthrene ∼ two-ring aromatics ≫ one-ring aromatic. Comparison with previous studies revealed that the relative reactivity of the aromatic compounds is strongly influenced by the nature of the catalyst. Multiple-component feed studies showed that phenanthrene and naphthalene strongly inhibited the tetralin hydrogenation rate; however, naphthalene and tetralin had no appreciable effect on phenanthrene conversion. Langmuir−Hinshelwood-type rate equations were used to describe the reaction kinetics with physically meaningful and well-identified parameter values. The inhibition was attributed to competitive adsorption and was described in the kinetic model by adsorption terms that were obtained from the multicomponent feed experiments.
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Elements of chemical reaction engineering
H. Scott Fogler · Chemical Engineering Science · 1987 · 3.1K citations