The gas-phase hydrogenation kinetics of ethylbenzene on Ni/Al2O3 was i
nvestigated in a differential microreactor at atmospheric pressure and
130-190 degrees C. Rapid deactivation of the catalyst complicated the
steady-state measurements. Reaction orders were near zero for the aro
matic compound and between 1.2 (130 degrees C) and 2.3 (190 degrees C)
for hydrogen. A rate maximum was observed at 160-175 degrees C, depen
ding on the concentration ratio of the reactants. Mechanistic modellin
g suggested that the reaction rate is governed by three steps of pairw
ise sequential addition of hydrogen atoms to adsorbed ethylbenzene. Th
e partially hydrogenated surface intermediates were proposed to have a
romatic character. The physical reasonability of the model parameters
was discussed.