Two types of laboratory structured reactors, which closely resemble industr
ial monolith catalysts, are theoretically and experimentally investigated f
or measurements of catalytic combustion kinetics under severe conditions: t
he annular reactor, consisting of a ceramic tube externally coated with a t
hin catalyst layer and coaxially placed in a slightly larger quartz tube; a
nd the metallic plate-type reactor, consisting of an assembled packet of me
tallic slabs coated with a ceramic catalytic layer.
After a brief description of an active coating deposition method suitable t
o provide structured reactors with adequate characteristics, a mathematical
model analysis of the annular reactor aimed at the design of the optimal c
onfiguration for kinetic investigations is first presented. The resulting a
dvantages, including: (i) negligible pressure drops; (ii) minimal impact of
diffusional Limitations in high temperature - high GHSV experiments; (iii)
effective dissipation of reaction heat are then experimentally demonstrate
d for the case of CH4 combustion over a PdO/gamma -Al2O3 catalyst with high
noble metal loading (10% w/w of Pd).
The feasibility of near-isothermal operation with the metallic plate-type r
eactor by an extremely effective dissipation of reaction heat through prope
r selection of highly conductive support materials and of the geometry of t
he metallic slabs is finally discussed and experimentally demonstrated for
the case of combustion of CO at high concentrations over a PdO/gamma -Al2O3
(3% w/w of Pd) catalyst. (C) 2001 Elsevier Science B.V, All rights reserve
d.