Prototype monolith catalysts with high intrinsic conductivity, consisting of extruded copper honeycombs washcoated with Pd/Al2O3 and suitable for industrial applications (∼25mm diameter) in multitubular externally cooled fixed-bed reactors, have been prepared and tested in both pure heat transfer and reactive experiments, using CO oxidation as a strongly exothermal model reaction. Measured temperature distributions indicated radial isothermal operation of the catalysts under the most severe conditions investigated. The limiting heat transfer resistance was located at the interface between the monolith and the reactor tube, and was significantly reduced by appropriate packaging methods controlling the clearance between the monolith and the tube. A detailed analysis, based on a 1D heterogeneous non-adiabatic model of the monolithic reactor, provided estimates of the monolith—wall heat transfer coefficient in the range 400–500W/(m2 K), which is regarded as very promising for industrial implementation.

Monolithic catalysis with high conductivity honeycomb supports for gas/solid exothermic reactions: characterization of the heat-transfer properties

GROPPI, GIANPIERO;TRONCONI, ENRICO
2004-01-01

Abstract

Prototype monolith catalysts with high intrinsic conductivity, consisting of extruded copper honeycombs washcoated with Pd/Al2O3 and suitable for industrial applications (∼25mm diameter) in multitubular externally cooled fixed-bed reactors, have been prepared and tested in both pure heat transfer and reactive experiments, using CO oxidation as a strongly exothermal model reaction. Measured temperature distributions indicated radial isothermal operation of the catalysts under the most severe conditions investigated. The limiting heat transfer resistance was located at the interface between the monolith and the reactor tube, and was significantly reduced by appropriate packaging methods controlling the clearance between the monolith and the tube. A detailed analysis, based on a 1D heterogeneous non-adiabatic model of the monolithic reactor, provided estimates of the monolith—wall heat transfer coefficient in the range 400–500W/(m2 K), which is regarded as very promising for industrial implementation.
2004
Catalyst support, Isothermal, Heat transfer, Packed bed, Monolithic catalysts, Reactor modeling, Multitubular
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/11311/271346
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