Oxidative Pyrolysis of Ethane

The effects of the addition of oxygen to the feed of an ethane steam cracker for ethylene production were investigated at industrial conditions by means of experiments and computer simulations. The oxidation of a small fraction of ethane feedstock in the cracking coil generates a significant amount...

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Bibliographic Details
Published inIndustrial & engineering chemistry research Vol. 36; no. 8; pp. 3248 - 3251
Main Authors Chen, Qi, Schweitzer, Erik J. A, Van Den Oosterkamp, Paul F, Berger, Rob J, De Smet, Carlo R. H, Marin, Guy B
Format Journal Article
LanguageEnglish
Published Washington, DC American Chemical Society 04.08.1997
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Summary:The effects of the addition of oxygen to the feed of an ethane steam cracker for ethylene production were investigated at industrial conditions by means of experiments and computer simulations. The oxidation of a small fraction of ethane feedstock in the cracking coil generates a significant amount of heat which can be used by the endothermic pyrolysis reactions. With this, the heat-transfer limitation in the industrial crackers is released. The addition of oxygen increases the conversion of ethane, while the yield to ethylene decreases slightly. Simulations indicate that the effects of the oxygen addition can be beneficial to industrial crackers in three manners:  decreased residence time or increased throughput, higher severity, or reduced tubeskin temperature and longer coil lifetime.
Bibliography:ark:/67375/TPS-3RS6SLFB-F
istex:81FB7CA8D741D260A3978EA13581D906A3EB664E
ISSN:0888-5885
1520-5045
DOI:10.1021/ie960585z