The liquid phase hydrogenation of phenylacetylene on pumice supported
palladium catalysts with a large range of metallic dispersions (14% <
D-x < 62%) has been carried out in a mechanically stirred glass reacto
r where any mass transfer effects are eliminated. A five parameters ma
thematical model has been used to analyze the kinetics. Three basic ro
utes, involving only surface species in the rate determining steps, co
ntributed to the mechanism of the reaction. The hydrogenation of pheny
lacetylene to styrene, with the pumice supported palladium catalysts,
shows good activity and selectivity. The reaction is structure insensi
tive in the whole range of the considered dispersions, in contrast to
that with other Pd catalysts on more traditional supports, which show
a marked decrease in activity and selectivity when dispersion of the m
etallic phase is higher than 20%.