This study focuses on assessing the performance and durability of three distinct catalysts, namely CoFe2O4/MgO and CoFe2O4/TiO2 and CoFe2O4/Al2O3 in the methane decomposition process. These catalysts were synthesized using a co-precipitation impregnation route. Their catalytic activity of methane decomposition was examined in a fixed-bed reactor at a temperature of 800 °C under atmospheric pressure. Various appropriate analytical techniques were employed to explore the physicochemical characteristics of both the fresh and spent catalysts. The SEM images, XRD and H2-TPR results of fresh catalysts revealed strong dependence on the support type. The XPS results confirm the presence CoFe2O4 species on the surface of supports. The CoFe2O4/MgO catalyst has a higher inversion degree compared with other catalysts as confirmed from Raman results. The methane conversions at the end of the reaction time (300 min) were found to be 66 %, 34 % and 2.48 %, while the rates of hydrogen formation corresponding to these methane conversions are 134.73 × 10−5, 68.25 × 10−5 and 8.80 × 10−5 mol H2 g−1 min−1 for CoFe2O4/MgO and CoFe2O4/TiO2 and CoFe2O4/Al2O3 catalysts, respectively. SEM images verified the existence of filamentous carbon on the surface of the spent CoFe2O4/MgO catalyst, whereas the spent CoFe2O4/TiO2 catalyst showed a mix of carbon chunks and filaments and fluffy carbon over the CoFe2O4/Al2O3 catalyst. Ultimately, the quantity of deposited carbon was significantly associated with catalytic activity, as they were 56, 46 and 4 wt% for the spent CoFe2O4/MgO, CoFe2O4/TiO2 and CoFe2O4/Al2O3 catalysts, respectively.
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