抄録
Steam reforming of methanol as a hydrogen producing catalytic reaction was studied in a Pd-membrane reactor. The activities, stabilities, and selectivities of Cu/ZnO, Ni/Al203, and Ru/Al203 catalysts were tested using a conventional fixed-bed flow reactor. Ni/Al203 catalyst showed the most stable activity at 723 K but relatively low hydrogen yield because of methanation. However, the hydrogen-permeable membrane reactor suppressed methanation, and hydrogen yield was enhanced compared with the conventional reactor. The membrane reactor was more efficient at higher temperatures and higher W/F.
本文言語 | English |
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ページ(範囲) | 93-98 |
ページ数 | 6 |
ジャーナル | Sekiyu Gakkaishi (Journal of the Japan Petroleum Institute) |
巻 | 46 |
号 | 2 |
出版ステータス | Published - 2003 3月 1 |
ASJC Scopus subject areas
- 燃料技術
- エネルギー工学および電力技術