Group VIII metals are found to present good behavior as hydrogenation
catalysts when supported on highly porous materials such as alumina. A
series of highly dispersed platinum catalysts supported on alumina ha
s been prepared by means of adsorption from solution, with platinum co
ntents varying from 0.5 to 3.0 wt %. The kinetic behavior of the catal
ysts has been analyzed for the liquid-phase hydrogenation of benzene i
n a stirred tank reactor, assuring a chemically-controlled regime for
stirring speed above 600 rpm and catalyst particle size below 0.08-0.1
6 mm in the studied conditions. For a constant dispersion, a certain a
mount of surface platinum has been found to remain inactive, either du
e to inaccessibility of the reagents or due to poisoning. As hydrogen
pressure increases, the reaction order shifts from 1 to 0. The apparen
t activation energy resulted in 72 kJ mol-1.