Abstract
A low-temperature ethanol reformer based on a cobalt catalyst for the production of hydrogen has been designed aiming the feed of a fuel cell for an autonomous low-scale power production unit. The reformer comprises three stages: ethanol dehydrogenation to acetaldehyde and hydrogen over SnO{sub 2} followed by acetaldehyde steam reforming over Co(Fe)/ZnO catalyst and water gas shift reaction. Kinetic data have been obtained under different experimental conditions and a dynamic model has been developed for a tubular reformer loaded with catalytic monoliths for the production of the hydrogen required to feed a 1 kW PEMFC. (author)
Garcia, Vanesa M;
Serra, Maria;
[1]
Lopez, Eduardo;
Llorca, Jordi
[2]
- Institut de Robotica i Informatica Industrial (CSIC-UPC), Llorens i Artigas 4-6, 08028 Barcelona (Spain)
- Institut de Tecniques Energetiques, Universitat Politecnica de Catalunya, Diagonal 647, ed. ETSEIB, 08028 Barcelona (Spain)
Citation Formats
Garcia, Vanesa M, Serra, Maria, Lopez, Eduardo, and Llorca, Jordi.
Dynamic modeling of a three-stage low-temperature ethanol reformer for fuel cell application.
Netherlands: N. p.,
2009.
Web.
doi:10.1016/J.JPOWSOUR.2008.12.055.
Garcia, Vanesa M, Serra, Maria, Lopez, Eduardo, & Llorca, Jordi.
Dynamic modeling of a three-stage low-temperature ethanol reformer for fuel cell application.
Netherlands.
https://doi.org/10.1016/J.JPOWSOUR.2008.12.055
Garcia, Vanesa M, Serra, Maria, Lopez, Eduardo, and Llorca, Jordi.
2009.
"Dynamic modeling of a three-stage low-temperature ethanol reformer for fuel cell application."
Netherlands.
https://doi.org/10.1016/J.JPOWSOUR.2008.12.055.
@misc{etde_21186650,
title = {Dynamic modeling of a three-stage low-temperature ethanol reformer for fuel cell application}
author = {Garcia, Vanesa M, Serra, Maria, Lopez, Eduardo, and Llorca, Jordi}
abstractNote = {A low-temperature ethanol reformer based on a cobalt catalyst for the production of hydrogen has been designed aiming the feed of a fuel cell for an autonomous low-scale power production unit. The reformer comprises three stages: ethanol dehydrogenation to acetaldehyde and hydrogen over SnO{sub 2} followed by acetaldehyde steam reforming over Co(Fe)/ZnO catalyst and water gas shift reaction. Kinetic data have been obtained under different experimental conditions and a dynamic model has been developed for a tubular reformer loaded with catalytic monoliths for the production of the hydrogen required to feed a 1 kW PEMFC. (author)}
doi = {10.1016/J.JPOWSOUR.2008.12.055}
journal = []
issue = {1}
volume = {192}
place = {Netherlands}
year = {2009}
month = {Jul}
}
title = {Dynamic modeling of a three-stage low-temperature ethanol reformer for fuel cell application}
author = {Garcia, Vanesa M, Serra, Maria, Lopez, Eduardo, and Llorca, Jordi}
abstractNote = {A low-temperature ethanol reformer based on a cobalt catalyst for the production of hydrogen has been designed aiming the feed of a fuel cell for an autonomous low-scale power production unit. The reformer comprises three stages: ethanol dehydrogenation to acetaldehyde and hydrogen over SnO{sub 2} followed by acetaldehyde steam reforming over Co(Fe)/ZnO catalyst and water gas shift reaction. Kinetic data have been obtained under different experimental conditions and a dynamic model has been developed for a tubular reformer loaded with catalytic monoliths for the production of the hydrogen required to feed a 1 kW PEMFC. (author)}
doi = {10.1016/J.JPOWSOUR.2008.12.055}
journal = []
issue = {1}
volume = {192}
place = {Netherlands}
year = {2009}
month = {Jul}
}