Numerical simulation of ion transport membrane reactors: Oxygen permeation and transport and fuel conversion

Ion transport membrane (ITM) based reactors have been suggested as a novel technology for several applications including fuel reforming and oxy-fuel combustion, which integrates air separation and fuel conversion while reducing complexity and the associated energy penalty. To utilize this technology...

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Bibliographic Details
Main Authors: Hong, Jongsup (Contributor), Kirchen, Patrick N. (Contributor), Ghoniem, Ahmed F. (Contributor)
Other Authors: Massachusetts Institute of Technology. Department of Mechanical Engineering (Contributor)
Format: Article
Language:English
Published: Elsevier, 2016-08-11T20:48:28Z.
Subjects:
Online Access:Get fulltext
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042 |a dc 
100 1 0 |a Hong, Jongsup  |e author 
100 1 0 |a Massachusetts Institute of Technology. Department of Mechanical Engineering  |e contributor 
100 1 0 |a Hong, Jongsup  |e contributor 
100 1 0 |a Kirchen, Patrick N.  |e contributor 
100 1 0 |a Ghoniem, Ahmed F.  |e contributor 
700 1 0 |a Kirchen, Patrick N.  |e author 
700 1 0 |a Ghoniem, Ahmed F.  |e author 
245 0 0 |a Numerical simulation of ion transport membrane reactors: Oxygen permeation and transport and fuel conversion 
260 |b Elsevier,   |c 2016-08-11T20:48:28Z. 
856 |z Get fulltext  |u http://hdl.handle.net/1721.1/103909 
520 |a Ion transport membrane (ITM) based reactors have been suggested as a novel technology for several applications including fuel reforming and oxy-fuel combustion, which integrates air separation and fuel conversion while reducing complexity and the associated energy penalty. To utilize this technology more effectively, it is necessary to develop a better understanding of the fundamental processes of oxygen transport and fuel conversion in the immediate vicinity of the membrane. In this paper, a numerical model that spatially resolves the gas flow, transport and reactions is presented. The model incorporates detailed gas phase chemistry and transport. The model is used to express the oxygen permeation flux in terms of the oxygen concentrations at the membrane surface given data on the bulk concentration, which is necessary for cases when mass transfer limitations on the permeate side are important and for reactive flow modeling. The simulation results show the dependence of oxygen transport and fuel conversion on the geometry and flow parameters including the membrane temperature, feed and sweep gas flow, oxygen concentration in the feed and fuel concentration in the sweep gas. 
520 |a King Fahd University of Petroleum and Minerals 
520 |a King Abdullah University of Science and Technology (KAUST) (grant number KSU-I1-010-01) 
546 |a en_US 
655 7 |a Article 
773 |t Journal of Membrane Science