The kinetics of the liquid-phase hydrogenation of naphthalene and tetralin (1,2,3,4-tetrahydronaphthalene) in decane was studied on a commercial nickel catalyst at 80−160 °C and 20−40
bar in a CSTR. The proposed kinetic model assumes three adsorption modes (π-, π/σ-, and
σ-adsorption), of which two are associative and one is dissociative. The associatively adsorbed
aromatic compounds are assumed to be active in hydrogenation, whereas the dissociative
adsorption leads to coke formation. Moreover, it is proposed that naphthalene adsorption occurs
on a single active site, whereas tetralin adsorption requires an ensemble of Ni atoms. This
explains the nonlinear decrease in the tetralin hydrogenation rate with catalyst deactivation,
whereas the naphthalene hydrogenation decreases linearly. The proposed reaction and deactivation mechanism is able to describe the main features of the observed kinetics, including the
formation of octalins (octahydronaphthalene), changes in the cis-to-trans selectivity of decalin
(decahydronaphthalene), and the difference between the naphthalene and tetralin hydrogenation
and deactivation rates.