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- Kusakabe Katsuki
- Department of Living Environmental Science, Fukuoka Women’s University
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- Mizoguchi Hitomi
- Department of Living Environmental Science, Fukuoka Women’s University
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Methane steam reforming (MSR) over a Rh-loaded Ce0.15Zr0.85O2 catalyst in a membrane reactor was investigated. An yttria-stabilized zirconia (YSZ) membrane used in the membrane reactor showed an ideal H2/N2 selectivity of 6.6 at a H2 permeance of 3.3 × 10–6 mol m–2 s–1 Pa–1 at 500°C. Methane conversions in the membrane reactor were higher than those in a packed bed reactor due to the sufficient permeation rate of hydrogen, which shifted the equilibrium, reaching 82% at 550°C. To evaluate the stability of a membrane reactor, the methane conversion was measured as a function of time. As a result, no significant change in methane conversion was evident at 500°C for 7 h.
収録刊行物
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- JOURNAL OF CHEMICAL ENGINEERING OF JAPAN
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JOURNAL OF CHEMICAL ENGINEERING OF JAPAN 39 (4), 444-447, 2006
公益社団法人 化学工学会
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詳細情報 詳細情報について
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- CRID
- 1390001204569158400
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- NII論文ID
- 10018112554
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- NII書誌ID
- AA00709658
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- ISSN
- 18811299
- 00219592
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- NDL書誌ID
- 7884347
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- 本文言語コード
- en
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- データソース種別
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- JaLC
- NDL
- Crossref
- CiNii Articles
- KAKEN
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- 抄録ライセンスフラグ
- 使用不可