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The catalytic performance of Ce-and La-promoted Ni/SBA-15 catalysts for syngas production from CO2 reforming of methane has been investigated in a fixed-bed reactor at stoichiometric feed composition. Both promoted and unpromoted catalysts possessed high BET surface area of 303-445 m 2 g -1 . Additionally, SBA-15 support had a relatively uniform rod-like shape with a diameter of about 0.55 µm and a reduction in the crystallite size of NiO phase from 27.0 to 19.1 nm was observed with promoterdoi:10.1016/j.proeng.2016.06.556 fatcat:nf7rcjvt4vex7enxhwxwnzyplm