Kinetic Modeling of the Heterogeneously Catalyzed Oxidation of Propene to Acrolein in a Catalytic Wall Reactor

Using data from isothermal investigations in a catalytic wall reactor (Redlingshöfer, H.; Kröcher, O.; Böck, W.; Huthmacher, K.; Emig, G. Ind. Eng. Chem. Res. 2002, 41, 1445), the kinetics of the highly exothermic vapor-phase oxidation of propene was determined by statistical parameter estimation. I...

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Published inIndustrial & engineering chemistry research Vol. 42; no. 22; pp. 5482 - 5488
Main Authors Redlingshöfer, Hubert, Fischer, Achim, Weckbecker, Christoph, Huthmacher, Klaus, Emig, Gerhard
Format Journal Article
LanguageEnglish
Published Washington, DC American Chemical Society 29.10.2003
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Abstract Using data from isothermal investigations in a catalytic wall reactor (Redlingshöfer, H.; Kröcher, O.; Böck, W.; Huthmacher, K.; Emig, G. Ind. Eng. Chem. Res. 2002, 41, 1445), the kinetics of the highly exothermic vapor-phase oxidation of propene was determined by statistical parameter estimation. It was shown that the oxidation of propene to acrolein follows a redox mechanism, with a change in the rate-determining step that depends on temperature. Two kinetic equations for the reduction and reoxidation regimes were necessary for a good fit to the experimental values. About a 3-fold higher activation energy for the reoxidation step and different propene and oxygen concentration dependencies of the rate equations in the two regimes were observed. An increasing water content improves catalyst reoxidation. This special catalytic effect was modeled by including an activity function. The kinetics of the byproducts acrylic acid, carbon oxides, formaldehyde, acetaldehyde, and acetic acid were considered with a reaction scheme consisting of 10 reactions. The model describes the experimental data very well. It includes 31 significant kinetic parameters.
AbstractList Using data from isothermal investigations in a catalytic wall reactor (Redlingshöfer, H.; Kröcher, O.; Böck, W.; Huthmacher, K.; Emig, G. Ind. Eng. Chem. Res. 2002, 41, 1445), the kinetics of the highly exothermic vapor-phase oxidation of propene was determined by statistical parameter estimation. It was shown that the oxidation of propene to acrolein follows a redox mechanism, with a change in the rate-determining step that depends on temperature. Two kinetic equations for the reduction and reoxidation regimes were necessary for a good fit to the experimental values. About a 3-fold higher activation energy for the reoxidation step and different propene and oxygen concentration dependencies of the rate equations in the two regimes were observed. An increasing water content improves catalyst reoxidation. This special catalytic effect was modeled by including an activity function. The kinetics of the byproducts acrylic acid, carbon oxides, formaldehyde, acetaldehyde, and acetic acid were considered with a reaction scheme consisting of 10 reactions. The model describes the experimental data very well. It includes 31 significant kinetic parameters.
Author Fischer, Achim
Redlingshöfer, Hubert
Emig, Gerhard
Weckbecker, Christoph
Huthmacher, Klaus
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Issue 22
Keywords Parameter estimation
Catalytic reaction
Catalytic reactor
Modeling
Acrolein
Propene
Statistical parameter
Water content
Oxidation
Kinetics
Kinetic parameter
Activation energy
Catalyst
Language English
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Snippet Using data from isothermal investigations in a catalytic wall reactor (Redlingshöfer, H.; Kröcher, O.; Böck, W.; Huthmacher, K.; Emig, G. Ind. Eng. Chem. Res....
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SubjectTerms Applied sciences
Catalysis
Catalytic reactions
Chemical engineering
Chemistry
Exact sciences and technology
General and physical chemistry
Reactors
Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry
Title Kinetic Modeling of the Heterogeneously Catalyzed Oxidation of Propene to Acrolein in a Catalytic Wall Reactor
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