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

doi:10.1016/S1566-7367(00)00014-5

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

研究成果: Article › 査読

62 被引用数 (Scopus)

抄録

Circulation of Ni_0.15Mg_0.85O 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.

本文言語	English
ページ（範囲）	11-15
ページ数	5
ジャーナル	Catalysis Communications
巻	2
号	1
DOI	https://doi.org/10.1016/S1566-7367(00)00014-5
出版ステータス	Published - 2001
外部発表	はい

ASJC Scopus subject areas

触媒
化学 (全般)
プロセス化学およびプロセス工学

文献へのアクセス

10.1016/S1566-7367(00)00014-5

他のファイルとリンク

引用スタイル

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

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.",

author = "Keiichi Tomishige and Yuichi Matsuo and Yasushi Sekine and Kaoru Fujimoto",

note = "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).",

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AU - Fujimoto, Kaoru

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AB - 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.

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