The hybrid catalytic combustor concept proposed by the authors has an
advantage concerned with catalyst durability, because the catalyst is
maintained below 1000 degrees C even for application to 1300 degrees C
class gas turbines. A full-scale hybrid catalytic combustor has been
designed for a 200 MW (1300 degrees C) class gas turbine. The catalyst
bed was 450 mm in diameter and consisted of a Pd/alumina washcoat on
a cordierite monolith. In experiments, the combustor has demonstrated
the capability of meeting the NOx emission level of SCR (selected cata
lytic reduction) during atmospheric pressure testing. To predict the c
atalyst performance at an elevated pressure, the characteristics of th
e catalyst were studied using a small scale reactor test, and a materi
al property test using a DTA/TGA-Q.MASS system. The catalyst showed a
higher activity in the oxidized state (PdO) than in the metallic state
(Pd). This activity difference was governed by the equilibrium of the
oxygen release from PdO in bulk. It was considered that oxidation rat
e of the metallic Pd in bulk was not so high and this caused self-osci
llation for the Pd catalyst around the temperature of the oxygen relea
se equilibrium. Even below the temperature of the oxygen release equil
ibrium, both surface and bulk (lattice) oxygen of the PdO was consumed
by the methane oxidation reaction, and resulted in a lack of surface
oxygen on the catalyst. This caused a reversible decrease in the catal
yst activity during combustion testing, and indicated that the oxygen
dissociation step was a rate limiting step in the catalytic combustion
.