INTERACTION OF KINETICS, DIFFUSION AND GEOMETRIC STRUCTURE OF PORE NETWORKS IN CATALYST SUPPORTS - A PERCOLATION THEORETICAL APPROACH TO HYDRODEMETALATION
C. Rieckmann et al., INTERACTION OF KINETICS, DIFFUSION AND GEOMETRIC STRUCTURE OF PORE NETWORKS IN CATALYST SUPPORTS - A PERCOLATION THEORETICAL APPROACH TO HYDRODEMETALATION, Hungarian journal of industrial chemistry, 25(2), 1997, pp. 137-145
A detailed analysis of geometric parameters of a catalyst pellet for a
hydrodemetallation reaction was carried out. A three-dimensional netw
ork of interconnected cylindrical pores was taken as a pore model, The
change of the pore space with time was analysed by a cluster counting
algorithm; It turned out that the reaction continues for a long time
after the percolation threshold has passed. In this example, the radii
of macropores are the most important parameters. Insights into the im
portance of different geometric parameters on the catalyst performance
could be obtained, which, in principle, cannot be obtained by continu
um models.