Methane Dry Reforming at High Temperature and Elevated Pressure: Impact of Gas-Phase Reactions

Catalytic dry reforming over a platinum-based catalyst is described experimentally and numerically in a laboratory pilot-plant flow reactor. The results reveal that coking in the upper part of the catalyst bed and at the entrance of the reactor occurs, depending on the composition of the reaction mi...

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Bibliographic Details

Published in:	Industrial & engineering chemistry research Vol. 52; no. 34; pp. 11920 - 11930
Main Authors:	Kahle, Lea C. S, Roussière, Thomas, Maier, Lubow, Herrera Delgado, Karla, Wasserschaff, Guido, Schunk, Stephan A, Deutschmann, Olaf
Format:	Journal Article
Language:	English
Published:	American Chemical Society 28-08-2013
Subjects:	Catalysts Coke Coking Drying Mathematical models Methane Reactors Reforming
Online Access:	Get full text
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