Details
Original language | English |
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Title of host publication | 21st European Symposium on Computer Aided Process Engineering |
Publisher | Elsevier BV |
Pages | 201-205 |
Number of pages | 5 |
ISBN (print) | 978-0-444-53711-9 |
Publication status | Published - 2011 |
Externally published | Yes |
Publication series
Name | Computer Aided Chemical Engineering |
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Publisher | Elsevier |
Volume | 29 |
ISSN (Print) | 1570-7946 |
Abstract
The preferential oxidation of CO from reformate gas in a spatially distributed electrochemical membrane reactor has been investigated. The reactor shows oscillations of the electric potential in space and time when operated in the galvanostatic mode. The operating behavior is complex and not straight-forward to predict, which hampers the application of classical methods for the design of such a reactor. Within the present work, a model-based approach is discussed to characterize the oscillations and their influence on the performance of the reactor.
Keywords
- Electrochemical membrane reactor, H production, Nonlinear dynamics
ASJC Scopus subject areas
- Chemical Engineering(all)
- General Chemical Engineering
- Computer Science(all)
- Computer Science Applications
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21st European Symposium on Computer Aided Process Engineering. Elsevier BV, 2011. p. 201-205 (Computer Aided Chemical Engineering; Vol. 29).
Research output: Chapter in book/report/conference proceeding › Conference contribution › Research › peer review
}
TY - GEN
T1 - Spatiotemporal pattern formation in an electrochemical membrane reactor during deep CO removal from reformate gas
AU - Hanke-Rauschenbach, Richard
AU - Kirsch, Sebastian
AU - Sundmacher, Kai
N1 - Copyright: Copyright 2011 Elsevier B.V., All rights reserved.
PY - 2011
Y1 - 2011
N2 - The preferential oxidation of CO from reformate gas in a spatially distributed electrochemical membrane reactor has been investigated. The reactor shows oscillations of the electric potential in space and time when operated in the galvanostatic mode. The operating behavior is complex and not straight-forward to predict, which hampers the application of classical methods for the design of such a reactor. Within the present work, a model-based approach is discussed to characterize the oscillations and their influence on the performance of the reactor.
AB - The preferential oxidation of CO from reformate gas in a spatially distributed electrochemical membrane reactor has been investigated. The reactor shows oscillations of the electric potential in space and time when operated in the galvanostatic mode. The operating behavior is complex and not straight-forward to predict, which hampers the application of classical methods for the design of such a reactor. Within the present work, a model-based approach is discussed to characterize the oscillations and their influence on the performance of the reactor.
KW - Electrochemical membrane reactor
KW - H production
KW - Nonlinear dynamics
KW - Electrochemical membrane reactor
KW - H2 production
KW - Nonlinear dynamics
UR - http://www.scopus.com/inward/record.url?scp=79958864871&partnerID=8YFLogxK
U2 - 10.1016/B978-0-444-53711-9.50041-9
DO - 10.1016/B978-0-444-53711-9.50041-9
M3 - Conference contribution
AN - SCOPUS:79958864871
SN - 978-0-444-53711-9
T3 - Computer Aided Chemical Engineering
SP - 201
EP - 205
BT - 21st European Symposium on Computer Aided Process Engineering
PB - Elsevier BV
ER -