The suitability of the nickel aluminate phase as an effective precursor for producing highly active and stable Ni/ alumina catalysts was investigated in the steam reforming of methane with a H 2 O/CH 4 ratio of 3 in the 450−650°C temperature range. Particularly, the effect of the preparation route, including dissolution followed by crystallization, coimpregnation, and coprecipitation, for obtaining either bulk or alumina-supported samples was analyzed. A special attention was paid to correlating the characteristics of the calcined catalytic precursors with a Ni content varying between 17 and 33 wt %, namely, textural properties, composition, nature, and relative abundance of the existing nickel phases (NiAl 2 O 4 and NiO), as well as reducibility, with the Ni crystallite size, dispersion, and metallic surface area obtained after a severe high-temperature reduction step (850°C). A high intrinsic activity was found for the coprecipitated catalysts. This route was also effective for increasing the available metallic surface area. The best reforming performance (with a methane conversion of 78−80% and yield of hydrogen close to 1.63 at 650°C and 38 400 cm 3 CH 4 g −1 h −1 ) was achieved by a reduced alumina-supported (17 wt % Ni)NiAl 2 O 4 catalyst and the bulk NiAl 2 O 4 catalysts prepared by coprecipitation.