The effect of the support structure on the stability a;nd catalytic activit
y in the CO2 reforming of methane was studied for the case of nickel-based
alumina catalysts, In addition to three commercial aluminas, four different
kinds of alumina were prepared, starting from the aluminum secbutoxide, as
candidate supports. The microstructural evolution and related phase transi
tions of the supports, catalyst precursors, and catalysts tested was follow
ed during both the preparation route and the mentioned reaction at 600 degr
ees C anti 1 bar of total pressure Strong influence of the support on the c
atalytic behavior was observed. In addition, satisfactory performance of a
specific methane steam reforming commercial catalyst is reported.