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- W2002873685 abstract "In this work, the role of hydrodynamics in an industrial-scale packed-bed catalytic reactor with a low tube/particle diameter ratio (dt/dp ∼ 3) and the role of redox dynamics of the catalyst surface together with the use of a catalyst activity profile are assessed on the heat transport during the partial oxidation of o-xylene on a V2O5/TiO2 catalyst. Temperature and concentration observations at different steady-state conditions are used to test the modeling approach, and reasonably good predictions are obtained when (1) the information contained in the heat-transport parameters, estimated from a boundary layer approximation to the hydrodynamics in the absence of chemical reactions [Ind. Eng. Chem. Res. 2007, 46 (23), 7426−7435], is used in the reactor model and (2) the redox catalyst dynamics, included in the reaction kinetics, is used, together with an empirical catalyst activity profile." @default.
- W2002873685 created "2016-06-24" @default.
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- W2002873685 date "2010-07-28" @default.
- W2002873685 modified "2023-10-12" @default.
- W2002873685 title "Modeling the Partial Oxidation of <i>o</i>-Xylene in an Industrial Packed-Bed Catalytic Reactor: The Role of Hydrodynamics and Catalyst Activity in the Heat Transport" @default.
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- W2002873685 doi "https://doi.org/10.1021/ie901720z" @default.
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