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

8 被引用数 (Scopus)

抄録

The application of the membrane reactor to steam reforming of methanol was studied as a hydrogen producing reaction. The activities, stabilities and selectivities of Cu/ZnO, Ni/Al2O3 and Ru/Al2O3 catalysts were tested using a conventional fixed-bed flow reactor. Ni/Al2O3 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 effective at higher temperatures and higher.

本文言語English
ページ(範囲)93-98
ページ数6
ジャーナルJournal of The Japan Petroleum Institute
46
3
DOI
出版ステータスPublished - 2008

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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