Temperature-programmed reduction (TPR) and continuous stepwise reducti
on-methanation (CSRM) have been used to identify and separate the acti
ve phases of Ni/Al2O3 catalyst. It is found that there are four hydrog
en consumption peaks representing four nickel species on Al2O3; the pe
ak temperatures for three of them are below 673 K when the reduction t
emperature does not exceed to 973 K. For the methanation of both CO an
d CO2, three distinct active phases are discovered, the activation tem
peratures of which coincide with the peak temperatures of the first th
ree TPR peaks, respectively. This indicates that different oxidized ni
ckel species exist on Al2O3 prior to reduction and form different acti
ve phases for the methanation of both CO and CO2 after reduction. The
methanation activities on each phase for both CO and CO2 in terms of C
H4 yield or initial methanation temperature and turnover number differ
significantly, Each phase also exhibits different activity for CO and
CO2 methanation. It is suggested that the mechanism of methanation fo
r CO or CO2 on different phases may vary, and that the mechanism for C
O and CO2 on the same phase may also vary. CSRM is convenient for sepa
rating different active phases for the methanation of both CO and CO2
on Ni/Al2O3 catalyst. (C) 1997 Academic Press.