A new route for obtaining 1,4-cyclooctadiene by catalytic isomerizatio
n of 1,5-cyclooctadiene at low temperature in presence of HZ in a thre
e-phase reactor is presented. Wei, Prater and Silvestri methods are us
ed for the kinetic studies. A comparison of the activity-selectivity p
atterns of the Pd/pumice catalysts with Pd on silica and Pt and Pd-Pt
on pumice catalysts is performed. Although Pt catalysts are not active
in the hydro-isomerization of 1,5-cyclooctadiene, the presence of sma
ll amount of Pt in Pd/pumice catalysts increases the yield to 1,4-cycl
ooctadiene. Besides the catalyst characteristics, temperature and H-2
pressure influence the production of 1,4-cyclooctadiene. A mechanism o
f the process is proposed.