The work presented in this paper was aimed at detecting, understanding and
modeling some critical behavior aspects of zeolite-containing diesel cataly
sts. An already available mathematical model for precious metal catalysts w
as used as a starting point. A specially designed set of experiments provid
ed the information needed to improve certain modeling features. New submode
ls were introduced to account for hydrocarbon and H2O adsorption, as well a
s diffusion limitations in the zeolite. The effect of flow maldistribution
during real world operation was investigated experimentally and computation
ally. Although a number of issues (especially regarding the DeNOx mechanism
s) are not yet fully resolved, significant progress was achieved as regards
the understanding and computational prediction of diesel catalyst operatio
n.