The
catalytic oxidations of acetylene, ethylene, and propylene
under transient and steady-state conditions were studied using model
Pd/Al2O3 and Pd/CeO2–ZrO2 monolith catalysts. Kinetics and light-off measurements highlight
the differences between the oxidation of each hydrocarbon. Acetylene
is strongly self-inhibiting and −1 order while the reaction
order with respect to ethylene is +1, both at temperatures below light-off.
Ethylene oxidation is moderately inhibited by oxygen at low temperatures
and ethylene at high temperatures. Mixture light-off experiments reveal
acetylene inhibits the oxidations of ethylene, propylene, and CO.
Light-off of the other species follow acetylene oxidation, which is
nearly unaffected by the other species. The Pd/CeO2–ZrO2 catalyst gives consistently higher conversion compared with
Pd/Al2O3 at the same Pd loading for each of
the individual oxidation reactions, although the negative-order kinetics
of acetylene is sustained. Oxidation of acetylene and mixtures containing
acetylene are enhanced with Pd/CeO2–ZrO2 compared to Pd/Al2O3. The effects of oxidative
or reductive pretreatment of the catalysts on species oxidations are
also evaluated. Mechanistic implications for the reactions are described
to guide kinetic model development. The findings highlight and clarify
inhibition effects during single and co-oxidation and offer insights
into optimizing the catalyst composition and its operation.