The present paper reviews three-dimensional random network models of cataly
st support structures. Multicomponent diffusion in the individual pores of
the network is described by the dusty-gas approach. In contrast to previous
publications, the present network model can be applied to any common react
ion kinetics. This becomes inevitable in order to make three-dimensional ne
twork models applicable to practical problems in the industry. The present
model is closely connected to measurable quantities which may be obtained b
y standard equipment. Examples of pore structure optimizations with respect
to various optimization criteria are given. Investigations of depositions
within the pores by percolation theoretical methods are described. Results
of simulations are compared to measurements in a single-pellet diffusion re
actor. The importance of surface diffusion is stressed. (C)1999 Elsevier Sc
ience B.V. All rights reserved.