Details
Originalsprache | Englisch |
---|---|
Seiten (von - bis) | 415-417 |
Seitenumfang | 3 |
Fachzeitschrift | DESALINATION |
Jahrgang | 199 |
Ausgabenummer | 1-3 |
Frühes Online-Datum | 8 Aug. 2006 |
Publikationsstatus | Elektronisch veröffentlicht (E-Pub) - 8 Aug. 2006 |
Abstract
A membrane reactor with perovskite hollow fibres in combination with a commercial steam reforming catalyst is used to produce in a long term scale synthesis gas with a methane conversion of about 96%, a CO selectivity of 95% and at a H2/CO ratio of 2. By having the whole perovskite hollow fibre at 875°C and adding steam, Ba carbonate and coke formations, respectively, could be avoided.
ASJC Scopus Sachgebiete
- Chemie (insg.)
- Chemische Verfahrenstechnik (insg.)
- Werkstoffwissenschaften (insg.)
- Umweltwissenschaften (insg.)
- Gewässerkunde und -technologie
- Ingenieurwesen (insg.)
- Maschinenbau
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in: DESALINATION, Jahrgang 199, Nr. 1-3, 08.08.2006, S. 415-417.
Publikation: Beitrag in Fachzeitschrift › Artikel › Forschung › Peer-Review
}
TY - JOUR
T1 - Perovskite hollow fibre membranes in the partial oxidation of methane to synthesis gas in a membrane reactor
AU - Caro, Jürgen
AU - Schiestel, Thomas
AU - Werth, Steffen
AU - Wang, Haihui
AU - Kleinert, Alexandra
AU - Kölsch, Peter
PY - 2006/8/8
Y1 - 2006/8/8
N2 - A membrane reactor with perovskite hollow fibres in combination with a commercial steam reforming catalyst is used to produce in a long term scale synthesis gas with a methane conversion of about 96%, a CO selectivity of 95% and at a H2/CO ratio of 2. By having the whole perovskite hollow fibre at 875°C and adding steam, Ba carbonate and coke formations, respectively, could be avoided.
AB - A membrane reactor with perovskite hollow fibres in combination with a commercial steam reforming catalyst is used to produce in a long term scale synthesis gas with a methane conversion of about 96%, a CO selectivity of 95% and at a H2/CO ratio of 2. By having the whole perovskite hollow fibre at 875°C and adding steam, Ba carbonate and coke formations, respectively, could be avoided.
KW - Catalytic membrane reactor
KW - Hollow fibre membrane
KW - Methane to syngas
KW - Perovskite
UR - http://www.scopus.com/inward/record.url?scp=33746757581&partnerID=8YFLogxK
U2 - 10.1016/j.desal.2006.03.206
DO - 10.1016/j.desal.2006.03.206
M3 - Article
AN - SCOPUS:33746757581
VL - 199
SP - 415
EP - 417
JO - DESALINATION
JF - DESALINATION
SN - 0011-9164
IS - 1-3
ER -