Intrinsic kinetic parameters are reported for the Pt/gamma-Al2O3 catalyzed
geometric isomerization of 1-hexene (P-c = 29.7 bar; T-c = 231 degrees C) u
nder conditions of steady catalyst activity. Deaerating the hexene feed, pr
etreating it in a bed of activated alumina to reduce the peroxide impuritie
s to 2 ppm or less, and passivating the reactor surface (by silicosteel coa
ting) reduce the formation of hexene oligomers (coke precursors) by about a
n order of magnitude. This, in conjunction with operation at supercritical
conditions (235-304 degrees C, 35-70 bar), results in steady isomerization
activity with no measurable coke laydown. Arrhenius plots of rate constants
, estimated from the steady isomerization rates, yield an intrinsic activat
ion energy of roughly 109 kJ/mol. This value is up to twofold greater than
those reported for similar reaction systems, but on a deactivating catalyst
s. Our results confirm that optimum conditions that maximize catalyst activ
ity and effectiveness factor exist in the near-critical region-with catalys
t activity and effectiveness factor.