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

Research output: Contribution to journalArticle

70 Citations (Scopus)

Abstract

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.

Original languageEnglish
Pages (from-to)439-445
Number of pages7
JournalCatalysis Today
Volume63
Issue number2-4
DOIs
Publication statusPublished - 2000 Dec 25
Externally publishedYes

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Methane
Reforming reactions
Fluidized beds
Solid solutions
Catalysts

ASJC Scopus subject areas

  • Catalysis
  • Process Chemistry and Technology

Cite this

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.

In: Catalysis Today, Vol. 63, No. 2-4, 25.12.2000, p. 439-445.

Research output: Contribution to journalArticle

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