Despite the high thermodynamic driving force to form coke under the re
action conditions applied Pt/ZrO2 and Rh supported on gamma-Al2O3 and
ZrO2 are active and stable catalysts for CO2/CH4 reforming. Using stea
dy state, transient kinetic measurements and physico-chemical characte
rization techniques have shown that the catalyst activity is determine
d by the available Pt-ZrO2 perimeter. Methane is decomposed on the met
al to CHx (average value of x = 2) and H-2. The main route to CO2 redu
ction occurs via initial formation of carbonate close to the metal-sup
port boundary. Carbon on the metal reduces that carbonate to formate b
y forming CO. The formate decomposes rapidly to CO and a surface hydro
xyl group. Hydroxyl groups recombine and form water or react further w
ith methane to CO and hydrogen (steam reforming). When the rate of met
hane decomposition and carbonate reduction are in balance, the catalyt
ic activity remains stable. In contrast, the activity of Rh is mainly
determined by the concentration of accessible surface atoms and a conc
erted metal catalyzed mechanism of methane decomposition and subsequen
t CO2 reduction dominates. The support plays a minimal role in that ch
emistry. (C) 1998 Academic Press.