The aim of this study is to compare pore structure characteristics of two i
ndustrial catalysts determined by standard methods of textural analysis (ph
ysical adsorption of nitrogen and mercury porosimetry) and selected methods
for obtaining parameters relevant to transport processes (multicomponent d
iffusion and permeation of gases). The Mean Transport Pore Model (MTPM) des
cribed diffusion and permeation and the Dusty Gas Model (DGM) described per
meation; models (represented as a boundary value problem for a set of ordin
ary differential equations) are based on Maxwell-Stefan diffusion equation
and Weber permeation law. Parameters of models are material constants of th
e porous solid and, thus, do not depend on conditions under which the trans
port processes take place. Both catalysts were mono- or bidispersed with me
an pore radii about 70 nm and 2000 nm; diffusion and permeation measurement
s were performed with four inert gases (H-2, He, N-2, and Ar).