N. Matsui et al., Reaction mechanisms of carbon dioxide reforming of methane with Ru-loaded lanthanum oxide catalyst, APP CATAL A, 179(1-2), 1999, pp. 247-256
A pulsed reaction technique was applied to discuss the effect of support on
the activities and mechanisms in the CO2 reforming of methane over Ru cata
lyst. The reaction was carried out using a fixed bed reactor equipped with
an on-line mass spectrometer. Four supports: La2O3, Y2O3 and ZrO2 which sho
wed high activity and Al2O3, commonly used one in the reforming reaction, w
ere compared when loaded with Ru.
After feeding CO2 at 600 degrees C, we introduced a pulse of CH4 over Ru/La
2O3 catalyst under Ar steady flow. We observed the response of CO which was
generated from the reaction with CHx on the ruthenium and the Ru-O-x forme
d during CO2 treatment or during the reaction of Ru-CHx with adsorbed CO2 o
nto the La2O3. Over Ru/Al2O3 catalyst, however, very small response of CO w
as observed. A pulse of (CO2)-C-13 was introduced under CH4 steady flow ove
r Ru/La2O3, Ru/Y2O3 and Ru/ZrO2 catalysts. Symmetrical (CO)-C-13 responses
were observed, but a small response of (CO)-C-12 from (CHx)-C-12 continued
to evolve after generation of (CO)-C-13 from (CO2)-C-13 ceased.
The following reaction cycle is believed to occur in the CO2 reforming of m
ethane on active supports: A part of metallic ruthenium reacted with CH4 to
give Ru-CHx; simultaneously ruthenium metal could be oxidized with CO2 to
give Ru-O-x and CO; and then, oxygen transfer from Ru-O-x to Ru-CHx took pl
ace to give CO and metallic ruthenium.
Distinct temperature increases in the catalyst bed for La2O3, Y2O3 and ZrO2
supports were observed with the introduction of CO2 pulses under Ar flow.
On the other hand, a very small increase in the temperature of the catalyst
bed was observed on Al2O3 These results indicate that CO2 reforming of CH4
with ruthenium loaded catalysts was strongly assisted by the activation of
CO2 adsorbed on the basic sites. (C) 1999 Elsevier Science B.V. All rights
reserved.