Methane reforming in a Pd/Ag membrane reactor was carried out. The operational limits for the steam-to-methane ratio are discussed. To avoid carbon formation, this ratio has to be higher in a Pd/Ag membrane reactor than in a conventional steam reforming tubular reactor.
Ethanol steam reforming in a membrane reactor with Pt-impregnated Knudsen membranes
β Scribed by Chang-Yeol Yu; Dong-Wook Lee; Sang-Jun Park; Kwan-Young Lee; Kew-Ho Lee
- Publisher
- Elsevier Science
- Year
- 2009
- Tongue
- English
- Weight
- 798 KB
- Volume
- 86
- Category
- Article
- ISSN
- 0926-3373
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