期刊
CHEMIE INGENIEUR TECHNIK
卷 86, 期 11, 页码 1901-1905出版社
WILEY-V C H VERLAG GMBH
DOI: 10.1002/cite.201400069
关键词
Ammonia oxidation; Membrane reactor; Methane aromatization; Process intensification
资金
- European Union
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.
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