抄録
The purpose of the present work is to establish the design method of methanol steam-reformer for application to chemical recuperation in a gas turbine system. The reaction rate of the methanol steam-reforming was measured with a small amount of catalyst using the gaseous mixture of methanol, water, hydrogen and carbon dioxide as a simulated product gas. The reaction rate equation could be expressed by power law of methanol mole fraction and total pressure. The reaction and heat transfer in the catalyst-packed bed was analyzed numerically using the reaction rate equation. The analytical results of temperature distribution and conversion were compared with the experimental results using a reforming tube. These results agreed well except for the region of high methanol conversion.
本文言語 | English |
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ページ | 569-576 |
ページ数 | 8 |
出版ステータス | Published - 1999 12月 1 |
外部発表 | はい |
イベント | The 1999 International Joint Power Generation Conference and ICOPE'99 - Burlingame, CA, USA 継続期間: 1999 7月 25 → 1999 7月 28 |
Other
Other | The 1999 International Joint Power Generation Conference and ICOPE'99 |
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City | Burlingame, CA, USA |
Period | 99/7/25 → 99/7/28 |
ASJC Scopus subject areas
- 工学(全般)