抜粋
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 |
| 巻 | 63 |
| 発行部数 | 2-4 |
| DOI | |
| 出版物ステータス | Published - 2000 12 25 |
ASJC Scopus subject areas
- Catalysis
- Chemistry(all)
フィンガープリント Autothermal CO<sub>2</sub> reforming of methane over NiO-MgO solid solution catalysts under pressurized condition: Effect of fluidized bed reactor and its promoting mechanism' の研究トピックを掘り下げます。これらはともに一意のフィンガープリントを構成します。
これを引用
Matsuo, Y., Yoshinaga, Y., Sekine, Y., Tomishige, K., & Fujimoto, K. (2000). Autothermal CO2 reforming of methane over NiO-MgO solid solution catalysts under pressurized condition: Effect of fluidized bed reactor and its promoting mechanism. Catalysis Today, 63(2-4), 439-445. https://doi.org/10.1016/S0920-5861(00)00489-2