Although Pt is the most appropriate catalyst for aqueous phase reforming (APR) of glycerol to generate H-2, it is expensive. We studied its possible minimisation to levels where acceptable H-2 yields are still maintained. When an additional catalytic metal, Ni, was introduced to our Pt/CeO2-Al2O3 catalyst, the Pt content could be reduced from 3 to 1 wt%, with a slight increase in H-2 production. In this study, Pt and Ni in various ratios were supported on alumina doped with 3 wt% ceria, and the resulting materials were characterised and tested as catalysts for the APR of glycerol. Amongst the catalysts tested, bimetallic 1Pt-6Ni/3CeAl (containing 1 wt% Pt and 6 wt% Ni) gave the highest H2 yield (86%) and gas-phase C yield (94%). Thus, although 1Pt-6Ni/3CeAl and our reported 3Pt/3CeAl catalyst produced almost same amount of H-2 (1.8 and 1.9 mmol, respectively) per gram of catalyst per hour, the latter produced three times as much H2 per gram of Pt per hour (195 mmol); this measure is crucial to the competitiveness of a catalyst in large-scale H-2 production. X-ray diffraction (XRD) patterns and thermogravimetric analyses of the spent catalysts showed no serious catalyst deactivation by carbon deposition after 30 h on stream, except in the case of Pt-free 6Ni/3CeAl, which ceased to produce H-2 after 15 h on stream. XRD and X-ray photoelectron spectroscopic analyses demonstrated that adding Ni impacted both the crystallite and electronic structure of Pt. These effects likely conspired to produce the high glycerol conversion and gas phase C yield and, ultimately, the high H-2 yield observed over 1Pt-6Ni/3CeAl.