Steam reforming of methanol on Ni/Al2O3 catalyst in a Pd-membrane reactor

Eiichi Kikuchi*, Shou Kawabe, Masahiko Matsukata

*この研究の対応する著者

研究成果: Article査読

12 被引用数 (Scopus)

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
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)
46
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

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