Co/CeO
2 (Co 7.5 wt.%), Ni/CeO
2 (Ni 7.5 wt.%) and Co–Ni/CeO
2 (Co 3.75 wt.%, Ni 3.75 wt.%) catalysts were prepared by surfactant assisted co-precipitation method. Samples were characterized by X-Ray diffraction, BET surface areas measurements, temperature programmed reduction and tested for the dry reforming of methane CH
4 + CO
2 → 2CO + 2H
2 in the temperature range 600–800 °C with a CH
4:CO
2:Ar 20:20:60 vol.% feed mixture and a total flow rate of 50 cm
3 min
−1 (GHSW = 30,000 mL g
−1 h
−1). The bimetallic Co–Ni/CeO
2 catalyst showed higher CH
4 conversion in comparison with monometallic systems in the whole temperature range, being 50% at 600 °C and 97% at 800 °C. H
2/CO selectivity decreased in the following order: Co–Ni/CeO
2 > Ni/CeO
2 > Co/CeO
2. Carbon deposition on spent catalysts was analyzed by thermal analysis (TG-DTA). After 20 h under stream at 750 °C, cobalt-containing catalysts, Co/CeO
2 and Co–Ni/CeO
2, showed a stable operation in presence of a deposited amorphous carbon of 6 wt.%, whereas Ni/CeO
2 showed an 8% decrease of catalytic activity due to a massive presence of amorphous and graphitic carbon (25 wt.%).
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