A novel problem, of diffusion resistance in porous particles that cata
lyze kinetically unstable reactions, is introduced, analyzed and simul
ated in order to unveil the possible spatiotemporal patterns in the di
rection perpendicular to the surface. Pore-diffusion resistance is a c
ore problem in chemical reaction engineering. The present problem is d
escribed mathematically by three variables: a very-fast and long-range
d pore-phase concentration, a fast and diffusing autocatalytic surface
species (activator) and a slow and localized surface activity. Unlike
homogeneous models of pore disfussion resistance, in which instabilit
ies emerge only with strong diffusion resistance, the present model ex
hibits oscillatory or excitable behavior even in the absence of that r
esistance. Patterns are generated by self-imposed concentration gradie
nts. A detailed kinetic model of a simple but reasonable reaction mech
anism is analyzed, but the qualitative results are expected to hold in
other similar kinetics. The catalyst particle is a three-dimensional
system and it may exhibit symmetry-breaking in the directions parallel
to the surface due to interaction between the fast diffusion of a flu
id-phase reactant and the slow solid-phase diffusivity of the activato
r. A thin catalyst can be described then by a one-dimensional reaction
-diffusion system that admits patterned solutions. We point our this p
ossibility, but refer to another work that investigates such patterns
in the general framework of patterns due to interaction of surface rea
ction and diffusion with gas-phase diffusion and convection. (C) 1996
American Institute of Physics.