The promotion effects of nickel catalyst of dry reforming with methane were
extensively investigated, by means of XRD, SEM, EDX, N-2-adsorption and H-
2-adsorption. XRD characterization indicated that good dispersion of nickel
oxide and NW promoter is achieved over gamma -Al2O3 support. Addition of N
W promoter effectively retards the formation of NiAl2O4 phase. SEM and EDX
analysis exhibited that the addition of rare-earth metal oxide CeCO2 effect
ively promotes the Ni metal dispersion on the surface of the catalysts desp
ite of undesirable self-dispersion of CeCO2 promoter. Furthermore, the nick
el component is gradually dispersed on the surface of the support following
the exposure to reaction gas mixture for a period of time. The addition of
MgO inhibited the self-dispersion and promotion effect of CeCO2 on Ni disp
ersion on the catalysts. H-2 chemisorption revealed that the addition of th
e alkaline oxide NW promoter significantly prohibits the metal dispersion o
n the catalyst. Inappropriate promoter addition can result in sharp decreas
e of the metal dispersion. NI-adsorption indicated that oxide promoter was
mostly concentrated on the outer layer of the alumina support while the nic
kel metal was generally dispersed in the support pores. Addition of promote
rs contributed to more reduction in mesopore volume.