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The effect of catalyst fluidization on the conversion of methane to syngas in methane reforming with CO 2 and H 2 O in the presence of O 2 under pressurized conditions was investigated over Ni and Pt catalysts. Methane and CO 2 conversion in the fluidized bed reactor was higher than those in the fixed bed reactor over Ni 0.15 Mg 0.85 O catalyst under...
The effect of fluidized bed reactor in autothermal CO 2 reforming of methane over NiO-MgO solid solution catalysts was investigated by comparing with fixed bed reactor. Methane conversion to syngas was drastically enhanced by using a fluidized bed reactor. The catalyst was reduced and oxidized repeatedly in fluidized bed reactor during the reaction. The enhancement of methane conversion is...
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