CO2 reforming of methane was studied over modified Ni/Al2O3 catalysts.
The metal modifiers were Co, Cu, Zr, Mn, Mo, Ti, Ag and Sn. Relative
to unmodified Ni/Al2O3, catalysts modified with Co, Cu and Zr showed s
lightly improved activity, while other promoters reduced the activity
of CO2 reforming. Mn-promoted catalyst showed a remarkable reduction i
n coke deposition, while entailing only a small reduction in catalytic
activity compared to unmodified catalyst. The catalysts prepared at h
igh calcination temperatures showed higher activity than those prepare
d at low calcination temperature. The Mn-promoted catalyst showed very
low coke deposition even in the absence of diluent gas and the activi
ty changed only slightly during 100 h operation.