Details
Originalsprache | Englisch |
---|---|
Seiten (von - bis) | 1901-1905 |
Seitenumfang | 5 |
Fachzeitschrift | Chemie-Ingenieur-Technik |
Jahrgang | 86 |
Ausgabenummer | 11 |
Publikationsstatus | Veröffentlicht - 22 Okt. 2014 |
Abstract
Two industrially interesting partial oxidations have been performed in catalytic membrane reactors with oxygen-transporting membrane: aromatization of natural gas and oxidation of ammonia to nitric oxide. In both reactions, the oxygen used has been separated from air through a perovskite membrane, which also is the catalyst for the ammonia oxidation. When conducting the methane aromatization in an oxygen-transporting membrane reactor, coke deposition is reduced and the aromatics yield is higher than that of a reference non-oxidative fixed-bed reactor.
ASJC Scopus Sachgebiete
- Chemie (insg.)
- Allgemeine Chemie
- Chemische Verfahrenstechnik (insg.)
- Allgemeine chemische Verfahrenstechnik
- Ingenieurwesen (insg.)
- Wirtschaftsingenieurwesen und Fertigungstechnik
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in: Chemie-Ingenieur-Technik, Jahrgang 86, Nr. 11, 22.10.2014, S. 1901-1905.
Publikation: Beitrag in Fachzeitschrift › Artikel › Forschung › Peer-Review
}
TY - JOUR
T1 - Catalytic membrane reactors - Lab curiosity or key enabling technology?
AU - Caro, Jürgen
PY - 2014/10/22
Y1 - 2014/10/22
N2 - Two industrially interesting partial oxidations have been performed in catalytic membrane reactors with oxygen-transporting membrane: aromatization of natural gas and oxidation of ammonia to nitric oxide. In both reactions, the oxygen used has been separated from air through a perovskite membrane, which also is the catalyst for the ammonia oxidation. When conducting the methane aromatization in an oxygen-transporting membrane reactor, coke deposition is reduced and the aromatics yield is higher than that of a reference non-oxidative fixed-bed reactor.
AB - Two industrially interesting partial oxidations have been performed in catalytic membrane reactors with oxygen-transporting membrane: aromatization of natural gas and oxidation of ammonia to nitric oxide. In both reactions, the oxygen used has been separated from air through a perovskite membrane, which also is the catalyst for the ammonia oxidation. When conducting the methane aromatization in an oxygen-transporting membrane reactor, coke deposition is reduced and the aromatics yield is higher than that of a reference non-oxidative fixed-bed reactor.
KW - Ammonia oxidation
KW - Membrane reactor
KW - Methane aromatization
KW - Process intensification
UR - http://www.scopus.com/inward/record.url?scp=84911928319&partnerID=8YFLogxK
U2 - 10.1002/cite.201400069
DO - 10.1002/cite.201400069
M3 - Article
AN - SCOPUS:84911928319
VL - 86
SP - 1901
EP - 1905
JO - Chemie-Ingenieur-Technik
JF - Chemie-Ingenieur-Technik
SN - 0009-286X
IS - 11
ER -