Mass
transfer analysis in any experimental system is fundamental
before studying its kinetics or optimizing a catalyst. The effect
of several variables, such as stirring rate, catalyst concentration
and particle size, hydrogen pressure, reaction temperature, polystyrene
concentration and average molecular weight, both from the experimental
and the theoretical point of view, have been studied in the catalytic
hydrocracking of polystyrene dissolved in decahydronaphthalene carried
out in a stirred tank with hydrogen and catalyst (0.58 wt % Pt/H-β)
in a slurry. The results show that the variables could be adequately
selected to prevent both gas–liquid and liquid–solid
mass transfer control. However, severe internal diffusion control
occurred as a consequence of polymer molecular dimensions that, in
practice, limits the reaction to the outer surface area of the catalyst.
Thus, catalyst optimization for this application, and catalytic processes
with polymer reactants in general, should be focused on maximizing
external surface area.