Details
| Originalsprache | Englisch |
|---|---|
| Seiten (von - bis) | 907-912 |
| Seitenumfang | 6 |
| Fachzeitschrift | Catalysis communications |
| Jahrgang | 7 |
| Ausgabenummer | 11 |
| Frühes Online-Datum | 20 Apr. 2006 |
| Publikationsstatus | Veröffentlicht - Nov. 2006 |
Abstract
A perovskite mixed conducting membrane made from the composition BaCoxFeyZrzO3-δ (BCFZ, x + y + z = 1.0) in a hollow fiber geometry was used to construct a membrane reactor for the partial oxidation of methane to syngas (CO + H2). In the membrane reactor without catalyst filling, the product gas contained mainly unreacted CH4 and O2 together with a few percent of CO2. After packing sufficient Ni-based catalyst around and behind the hollow fiber membrane, syngas (H2 + CO) was observed. At 925 °C, the CO selectivity reached about 97% with CH4 conversion of 96%. The possible reaction pathways were proposed to be an oxidation-reforming process.
ASJC Scopus Sachgebiete
- Chemische Verfahrenstechnik (insg.)
- Katalyse
- Chemie (insg.)
- Chemische Verfahrenstechnik (insg.)
- Prozesschemie und -technologie
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in: Catalysis communications, Jahrgang 7, Nr. 11, 11.2006, S. 907-912.
Publikation: Beitrag in Fachzeitschrift › Artikel › Forschung › Peer-Review
}
TY - JOUR
T1 - Partial oxidation of methane to syngas in a perovskite hollow fiber membrane reactor
AU - Wang, Haihui
AU - Tablet, Cristina
AU - Schiestel, Thomas
AU - Werth, Steffen
AU - Caro, Jürgen
PY - 2006/11
Y1 - 2006/11
N2 - A perovskite mixed conducting membrane made from the composition BaCoxFeyZrzO3-δ (BCFZ, x + y + z = 1.0) in a hollow fiber geometry was used to construct a membrane reactor for the partial oxidation of methane to syngas (CO + H2). In the membrane reactor without catalyst filling, the product gas contained mainly unreacted CH4 and O2 together with a few percent of CO2. After packing sufficient Ni-based catalyst around and behind the hollow fiber membrane, syngas (H2 + CO) was observed. At 925 °C, the CO selectivity reached about 97% with CH4 conversion of 96%. The possible reaction pathways were proposed to be an oxidation-reforming process.
AB - A perovskite mixed conducting membrane made from the composition BaCoxFeyZrzO3-δ (BCFZ, x + y + z = 1.0) in a hollow fiber geometry was used to construct a membrane reactor for the partial oxidation of methane to syngas (CO + H2). In the membrane reactor without catalyst filling, the product gas contained mainly unreacted CH4 and O2 together with a few percent of CO2. After packing sufficient Ni-based catalyst around and behind the hollow fiber membrane, syngas (H2 + CO) was observed. At 925 °C, the CO selectivity reached about 97% with CH4 conversion of 96%. The possible reaction pathways were proposed to be an oxidation-reforming process.
KW - Hollow fiber
KW - Membrane reactor
KW - Mixed conductor
KW - Perovskite
KW - POM
KW - Syngas
UR - http://www.scopus.com/inward/record.url?scp=33748928811&partnerID=8YFLogxK
U2 - 10.1016/j.catcom.2006.03.023
DO - 10.1016/j.catcom.2006.03.023
M3 - Article
AN - SCOPUS:33748928811
VL - 7
SP - 907
EP - 912
JO - Catalysis communications
JF - Catalysis communications
SN - 1566-7367
IS - 11
ER -