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The autothermal reforming of methane to syngas has been carried out in a reactor charged with both a Ni (15 wt%)-Ru (1 wt%)/-MgO metallic monolith catalyst and an electrically-heated convertor (EHC). The standalone type reactor has a start-up time of less than 2 min with the reactant gas of fed to the autothermal reactor. The and ratio governed the methane conversion and temperature profile of reactor. The reactor temperature increased as the reaction shifted from endothermic to exothermic reaction with decreasing ratio. Also the amount of in the products increases with increasing ratio due to water gas shift reaction. The 97% of conversion was obtained and the reactor temperature was maintained at the condition of $GHSV

Autothermal Reforming Reaction at Fuel Process Systems of 1Nm3/h

Autothermal Reforming Reaction at Fuel Process Systems of 1Nm³/h