The relationship between molecular structure and hydrogenation reactiv
ity in heavy oil hydroprocessing was sought via the elucidation of the
controlling reaction pathways and kinetics of one-, two-, three-, and
four-fused ring compounds. Hydrogenation reactions of o-xylene, tetra
lin, naphthalene, phenanthrene, anthracene, pyrene, and chrysene and t
heir multicomponent mixtures were studied in cyclohexane solvent using
a presulfided CoMo/Al2O3 catalyst in an 1-L batch autoclave at P-H2 =
68.1 atm and T = 350 degrees C. Quantitative network analysis allowed
estimation of 45 hydrogenation rate; parameters and an equal number o
f equilibrium ratios for 36 aromatic and hydroaromatic compounds. Thes
e values were then used in the evaluation of five adsorption parameter
s for aromatic ring number-based lumps from the multicomponent mixture
experiments. Three classes of hydrogenation were discerned, based on
the magnitude of numerator rate parameters. The adsorption parameters
clearly increased with increasing aromatic ring number.