The influence of operating parameters over dry reforming of methane reaction was evaluated using a Ni-based catalyst obtained after calcination of a hydrotalcite-like precursor. The studied variables were mass to flow ratio (W/F), reaction temperature and CO2/CH4 ratio. Maximum methane and carbon dioxide conversions were achieved at W/F ratios above 0.21 g h L-1. The higher the W/F ratio was, the lower amount of water was formed, which led to a higher H-2/CO ratio. The increase in reaction temperature produced an increase in conversions. Water concentration in the outlet stream showed a maximum at 600 degrees C. At this temperature, reverse water gas-shift reaction (RWGS) was favoured because it is endothermic. However, steam reforming and carbon gasification were also favoured and they consumed great part of the water produced. CO2/CH4 ratios above 1 led to a higher CH4 conversion but selectivity to hydrogen decreased because RWGS reaction was favoured. When CO2/CH4 was below unity, CH4 conversion decreased but less amount of water was produced so a higher H-2 selectivity was achieved. The catalyst exhibited good stability over dry reforming of methane under all the tested conditions, which may be ascribed to its high basicity. This property improved CO2 adsorption and then RWGS reaction and carbon gasification. Copyright (C) 2013, Hydrogen Energy Publications, LLC. Published by Elsevir Ltd. All rights reserved.