Autothermal CO2 reforming of methane over NiO-MgO solid solution catalysts under pressurized condition. Effect of fluidized bed reactor and its promoting mechanism

Yuichi Matsuo, Yusuke Yoshinaga, Yasushi Sekine, Keiichi Tomishige, Kaoru Fujimoto

研究成果: Article

70 引用 (Scopus)

抄録

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.

元の言語English
ページ(範囲)439-445
ページ数7
ジャーナルCatalysis Today
63
発行部数2-4
DOI
出版物ステータスPublished - 2000 12 25
外部発表Yes

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Methane
Reforming reactions
Fluidized beds
Solid solutions
Catalysts

ASJC Scopus subject areas

  • Catalysis
  • Process Chemistry and Technology

これを引用

Autothermal CO2 reforming of methane over NiO-MgO solid solution catalysts under pressurized condition. Effect of fluidized bed reactor and its promoting mechanism. / Matsuo, Yuichi; Yoshinaga, Yusuke; Sekine, Yasushi; Tomishige, Keiichi; Fujimoto, Kaoru.

:: Catalysis Today, 巻 63, 番号 2-4, 25.12.2000, p. 439-445.

研究成果: Article

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