Effective methane reforming with CO2 and O2 under pressurized condition using NiO-MgO and fluidized bed reactor

Keiichi Tomishige, Yuichi Matsuo, Yasushi Sekine, Kaoru Fujimoto

Research output: Contribution to journalArticle

61 Citations (Scopus)

Abstract

Circulation of Ni0.15Mg0.85O catalyst particles in the fluidized bed reactor gave much higher CH4 conversion in methane reforming with CO2 and O2 under pressurized condition than the case of the catalyst without moving in the fixed bed reactor. In addition, circulation of the catalyst particles in the fluidized bed reactor inhibited carbon deposition which is the serious problem in methane reforming.

Original languageEnglish
Pages (from-to)11-15
Number of pages5
JournalCatalysis Communications
Volume2
Issue number1
Publication statusPublished - 2001
Externally publishedYes

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Methane
Reforming reactions
Fluidized beds
Catalysts
Carbon

ASJC Scopus subject areas

  • Catalysis
  • Process Chemistry and Technology

Cite this

Effective methane reforming with CO2 and O2 under pressurized condition using NiO-MgO and fluidized bed reactor. / Tomishige, Keiichi; Matsuo, Yuichi; Sekine, Yasushi; Fujimoto, Kaoru.

In: Catalysis Communications, Vol. 2, No. 1, 2001, p. 11-15.

Research output: Contribution to journalArticle

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