Details
Original language | English |
---|---|
Pages (from-to) | 415-417 |
Number of pages | 3 |
Journal | DESALINATION |
Volume | 199 |
Issue number | 1-3 |
Early online date | 8 Aug 2006 |
Publication status | Published - 20 Nov 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.
Keywords
- Catalytic membrane reactor, Hollow fibre membrane, Methane to syngas, Perovskite
ASJC Scopus subject areas
- Chemistry(all)
- General Chemistry
- Chemical Engineering(all)
- General Chemical Engineering
- Materials Science(all)
- General Materials Science
- Environmental Science(all)
- Water Science and Technology
- Engineering(all)
- Mechanical Engineering
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In: DESALINATION, Vol. 199, No. 1-3, 20.11.2006, p. 415-417.
Research output: Contribution to journal › Article › Research › 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 - 2006/11/20
Y1 - 2006/11/20
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 -