Karaismailoğlu, MeltemFigen, Halit ErenBaykara, Sema Z.2021-01-082021-01-0820200360-3199https://doi.org/10.1016/j.ijhydene.2020.07.219https://hdl.handle.net/20.500.12846/316Catalytic approach for methane decomposition can be seriously considered as a promising process for COx free hydrogen generation. In this study, catalytic methane decomposition was performed using Fe-based catalysts, and catalytic performance tests were carried out in a CH4:N2 flow at 750 and 800 °C. The analyses of reaction products were carried out by a mass spectrometer. For the preparation of Fe-based catalysts, sol-gel method was utilized. Yttria (Y2O3) and alumina (Al2O3) were used as support materials. Theoretical molar ratios (Fe2O3/Y2O3/Al2O3) of the samples C1–C5 were 1:0:0, 1:1:0, 1:1:5, 2:1:4 and 3:1:6, respectively. The characterization analyses of fresh and spent catalysts were performed with XRD, SEM, TPR, TG-FTIR and BET surface analysis techniques. Surface basicity of catalysts was determined via CO2-TPD measurements. In the presence of Fe2O3/Y2O3 and Fe2O3/Y2O3/Al2O3 catalysts, methane conversions of 29% and 4% were achieved at 750 °C. Adding alumina into Fe2O3/Y2O3 catalyst leads to the formation of garnet type crystal structure which reduces catalytic activity. © 2020 Hydrogen Energy Publications LLCeninfo:eu-repo/semantics/closedAccessCatalytic methane decompositionFe-based catalystHydrogenArticle456010.1016/j.ijhydene.2020.07.2193477334782Q2Q1WOS:0006091616000202-s2.0-85089706539