TY - JOUR
T1 - Autothermal CO2 reforming of methane over NiO-MgO solid solution catalysts under pressurized condition
T2 - Effect of fluidized bed reactor and its promoting mechanism
AU - Matsuo, Yuichi
AU - Yoshinaga, Yusuke
AU - Sekine, Yasushi
AU - Tomishige, Keiichi
AU - Fujimoto, Kaoru
N1 - Funding Information:
A part of this research has been supported by the Future Program of Japan Society for the Promotion of Science under the Project “Synthesis of Ecological High Quality of Transportation Fuels” (JSPS-RFTF98P01001).
PY - 2000/12/25
Y1 - 2000/12/25
N2 - The effect of fluidized bed reactor in autothermal CO2 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 related to the catalyst reducibility.
AB - The effect of fluidized bed reactor in autothermal CO2 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 related to the catalyst reducibility.
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U2 - 10.1016/S0920-5861(00)00489-2
DO - 10.1016/S0920-5861(00)00489-2
M3 - Article
AN - SCOPUS:0034517404
VL - 63
SP - 439
EP - 445
JO - Catalysis Today
JF - Catalysis Today
SN - 0920-5861
IS - 2-4
ER -