Ethanol catalytic membrane reformer for direct PEM FC feeding
- Autores
- Koch, Reinhold; Lopez, Eduardo; Divins, Núria J.; Allué, Miguel; Jossen, Andreas; Riera, Jordi; Llorca, Jordi
- Año de publicación
- 2013
- Idioma
- inglés
- Tipo de recurso
- artículo
- Estado
- versión publicada
- Descripción
- In this paper an ethanol reformer based on catalytic steam reforming with a catalytic honeycomb loaded with RhPd/CeO2 and palladium separation membranes with an area of 30.4 cm2 has been used to generate a pure hydrogen stream of up to 100 ml/min to feed a PEM fuel cell with an active area of 5 cm2. The fuel reformer behavior has been extensively studied under different temperature, ethanolewater flow rate and gas pressure at a fixed S/C ratio of 1.6 (molar). The hydrogen yield has been controlled by acting upon the ethanol-water fuel flow and gas pressure. A mathematical model of the ethanol reformer has been developed and an adaptive and predictive control has been implemented on a real time system to take account of its nonlinear behavior. With this control the response time of the reformer can be reduced by a factor of 7 down to 8 s. The improved dynamics of the controlled reformer match better the quickly changing hydrogen demands of fuel cells. They reached a magnitude where costly hydrogen buffers between the reformer and the fuel cell can be omitted and an electric buffer at the output of the fuel cell is sufficient.
Fil: Koch, Reinhold. Universitat Technical Zu Munich;
Fil: Lopez, Eduardo. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico - CONICET - Bahia Blanca. Planta Piloto de Ingenieria Quimica (i); Argentina;
Fil: Divins, Núria J.. Institut de Têcniques Energetiques, Universitat Politecnica de Catalunya, España;
Fil: Allué, Miguel. Institut de Robótica i Informática Industrial; España;
Fil: Jossen, Andreas. Institute for Electrical Energy Storage Technology. Technische Universitat Munchen; Alemania;
Fil: Riera, Jordi. Institut de Robótica i Informática Industrial; España;
Fil: Llorca, Jordi. Institut de Têcniques Energetiques, Universitat Politecnica de Catalunya, España; - Materia
-
Ethanol steam reforming
Metal membrane
PEM fuel cell
Sensitivity analysis
Dynamic modeling
Reformer control - Nivel de accesibilidad
- acceso abierto
- Condiciones de uso
- https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
- Repositorio
.jpg)
- Institución
- Consejo Nacional de Investigaciones Científicas y Técnicas
- OAI Identificador
- oai:ri.conicet.gov.ar:11336/1086
Ver los metadatos del registro completo
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Ethanol catalytic membrane reformer for direct PEM FC feedingKoch, ReinholdLopez, EduardoDivins, Núria J.Allué, MiguelJossen, AndreasRiera, JordiLlorca, JordiEthanol steam reformingMetal membranePEM fuel cellSensitivity analysisDynamic modelingReformer controlhttps://purl.org/becyt/ford/2https://purl.org/becyt/ford/2.4In this paper an ethanol reformer based on catalytic steam reforming with a catalytic honeycomb loaded with RhPd/CeO2 and palladium separation membranes with an area of 30.4 cm2 has been used to generate a pure hydrogen stream of up to 100 ml/min to feed a PEM fuel cell with an active area of 5 cm2. The fuel reformer behavior has been extensively studied under different temperature, ethanolewater flow rate and gas pressure at a fixed S/C ratio of 1.6 (molar). The hydrogen yield has been controlled by acting upon the ethanol-water fuel flow and gas pressure. A mathematical model of the ethanol reformer has been developed and an adaptive and predictive control has been implemented on a real time system to take account of its nonlinear behavior. With this control the response time of the reformer can be reduced by a factor of 7 down to 8 s. The improved dynamics of the controlled reformer match better the quickly changing hydrogen demands of fuel cells. They reached a magnitude where costly hydrogen buffers between the reformer and the fuel cell can be omitted and an electric buffer at the output of the fuel cell is sufficient.Fil: Koch, Reinhold. Universitat Technical Zu Munich;Fil: Lopez, Eduardo. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico - CONICET - Bahia Blanca. Planta Piloto de Ingenieria Quimica (i); Argentina;Fil: Divins, Núria J.. Institut de Têcniques Energetiques, Universitat Politecnica de Catalunya, España;Fil: Allué, Miguel. Institut de Robótica i Informática Industrial; España;Fil: Jossen, Andreas. Institute for Electrical Energy Storage Technology. Technische Universitat Munchen; Alemania;Fil: Riera, Jordi. Institut de Robótica i Informática Industrial; España;Fil: Llorca, Jordi. Institut de Têcniques Energetiques, Universitat Politecnica de Catalunya, España;Pergamon-elsevier Science Ltd2013-02info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionhttp://purl.org/coar/resource_type/c_6501info:ar-repo/semantics/articuloapplication/pdfapplication/pdfhttp://hdl.handle.net/11336/1086Koch, Reinhold; Lopez, Eduardo; Divins, Núria J.; Allué, Miguel; Jossen, Andreas; et al.; Ethanol catalytic membrane reformer for direct PEM FC feeding; Pergamon-elsevier Science Ltd; International Journal Of Hydrogen Energy; 38; 14; 2-2013; 5605-56150360-3199enginfo:eu-repo/semantics/openAccesshttps://creativecommons.org/licenses/by-nc-sa/2.5/ar/reponame:CONICET Digital (CONICET)instname:Consejo Nacional de Investigaciones Científicas y Técnicas2025-10-15T15:04:42Zoai:ri.conicet.gov.ar:11336/1086instacron:CONICETInstitucionalhttp://ri.conicet.gov.ar/Organismo científico-tecnológicoNo correspondehttp://ri.conicet.gov.ar/oai/requestdasensio@conicet.gov.ar; lcarlino@conicet.gov.arArgentinaNo correspondeNo correspondeNo correspondeopendoar:34982025-10-15 15:04:43.086CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicasfalse |
| dc.title.none.fl_str_mv |
Ethanol catalytic membrane reformer for direct PEM FC feeding |
| title |
Ethanol catalytic membrane reformer for direct PEM FC feeding |
| spellingShingle |
Ethanol catalytic membrane reformer for direct PEM FC feeding Koch, Reinhold Ethanol steam reforming Metal membrane PEM fuel cell Sensitivity analysis Dynamic modeling Reformer control |
| title_short |
Ethanol catalytic membrane reformer for direct PEM FC feeding |
| title_full |
Ethanol catalytic membrane reformer for direct PEM FC feeding |
| title_fullStr |
Ethanol catalytic membrane reformer for direct PEM FC feeding |
| title_full_unstemmed |
Ethanol catalytic membrane reformer for direct PEM FC feeding |
| title_sort |
Ethanol catalytic membrane reformer for direct PEM FC feeding |
| dc.creator.none.fl_str_mv |
Koch, Reinhold Lopez, Eduardo Divins, Núria J. Allué, Miguel Jossen, Andreas Riera, Jordi Llorca, Jordi |
| author |
Koch, Reinhold |
| author_facet |
Koch, Reinhold Lopez, Eduardo Divins, Núria J. Allué, Miguel Jossen, Andreas Riera, Jordi Llorca, Jordi |
| author_role |
author |
| author2 |
Lopez, Eduardo Divins, Núria J. Allué, Miguel Jossen, Andreas Riera, Jordi Llorca, Jordi |
| author2_role |
author author author author author author |
| dc.subject.none.fl_str_mv |
Ethanol steam reforming Metal membrane PEM fuel cell Sensitivity analysis Dynamic modeling Reformer control |
| topic |
Ethanol steam reforming Metal membrane PEM fuel cell Sensitivity analysis Dynamic modeling Reformer control |
| purl_subject.fl_str_mv |
https://purl.org/becyt/ford/2 https://purl.org/becyt/ford/2.4 |
| dc.description.none.fl_txt_mv |
In this paper an ethanol reformer based on catalytic steam reforming with a catalytic honeycomb loaded with RhPd/CeO2 and palladium separation membranes with an area of 30.4 cm2 has been used to generate a pure hydrogen stream of up to 100 ml/min to feed a PEM fuel cell with an active area of 5 cm2. The fuel reformer behavior has been extensively studied under different temperature, ethanolewater flow rate and gas pressure at a fixed S/C ratio of 1.6 (molar). The hydrogen yield has been controlled by acting upon the ethanol-water fuel flow and gas pressure. A mathematical model of the ethanol reformer has been developed and an adaptive and predictive control has been implemented on a real time system to take account of its nonlinear behavior. With this control the response time of the reformer can be reduced by a factor of 7 down to 8 s. The improved dynamics of the controlled reformer match better the quickly changing hydrogen demands of fuel cells. They reached a magnitude where costly hydrogen buffers between the reformer and the fuel cell can be omitted and an electric buffer at the output of the fuel cell is sufficient. Fil: Koch, Reinhold. Universitat Technical Zu Munich; Fil: Lopez, Eduardo. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico - CONICET - Bahia Blanca. Planta Piloto de Ingenieria Quimica (i); Argentina; Fil: Divins, Núria J.. Institut de Têcniques Energetiques, Universitat Politecnica de Catalunya, España; Fil: Allué, Miguel. Institut de Robótica i Informática Industrial; España; Fil: Jossen, Andreas. Institute for Electrical Energy Storage Technology. Technische Universitat Munchen; Alemania; Fil: Riera, Jordi. Institut de Robótica i Informática Industrial; España; Fil: Llorca, Jordi. Institut de Têcniques Energetiques, Universitat Politecnica de Catalunya, España; |
| description |
In this paper an ethanol reformer based on catalytic steam reforming with a catalytic honeycomb loaded with RhPd/CeO2 and palladium separation membranes with an area of 30.4 cm2 has been used to generate a pure hydrogen stream of up to 100 ml/min to feed a PEM fuel cell with an active area of 5 cm2. The fuel reformer behavior has been extensively studied under different temperature, ethanolewater flow rate and gas pressure at a fixed S/C ratio of 1.6 (molar). The hydrogen yield has been controlled by acting upon the ethanol-water fuel flow and gas pressure. A mathematical model of the ethanol reformer has been developed and an adaptive and predictive control has been implemented on a real time system to take account of its nonlinear behavior. With this control the response time of the reformer can be reduced by a factor of 7 down to 8 s. The improved dynamics of the controlled reformer match better the quickly changing hydrogen demands of fuel cells. They reached a magnitude where costly hydrogen buffers between the reformer and the fuel cell can be omitted and an electric buffer at the output of the fuel cell is sufficient. |
| publishDate |
2013 |
| dc.date.none.fl_str_mv |
2013-02 |
| dc.type.none.fl_str_mv |
info:eu-repo/semantics/article info:eu-repo/semantics/publishedVersion http://purl.org/coar/resource_type/c_6501 info:ar-repo/semantics/articulo |
| format |
article |
| status_str |
publishedVersion |
| dc.identifier.none.fl_str_mv |
http://hdl.handle.net/11336/1086 Koch, Reinhold; Lopez, Eduardo; Divins, Núria J.; Allué, Miguel; Jossen, Andreas; et al.; Ethanol catalytic membrane reformer for direct PEM FC feeding; Pergamon-elsevier Science Ltd; International Journal Of Hydrogen Energy; 38; 14; 2-2013; 5605-5615 0360-3199 |
| url |
http://hdl.handle.net/11336/1086 |
| identifier_str_mv |
Koch, Reinhold; Lopez, Eduardo; Divins, Núria J.; Allué, Miguel; Jossen, Andreas; et al.; Ethanol catalytic membrane reformer for direct PEM FC feeding; Pergamon-elsevier Science Ltd; International Journal Of Hydrogen Energy; 38; 14; 2-2013; 5605-5615 0360-3199 |
| dc.language.none.fl_str_mv |
eng |
| language |
eng |
| dc.rights.none.fl_str_mv |
info:eu-repo/semantics/openAccess https://creativecommons.org/licenses/by-nc-sa/2.5/ar/ |
| eu_rights_str_mv |
openAccess |
| rights_invalid_str_mv |
https://creativecommons.org/licenses/by-nc-sa/2.5/ar/ |
| dc.format.none.fl_str_mv |
application/pdf application/pdf |
| dc.publisher.none.fl_str_mv |
Pergamon-elsevier Science Ltd |
| publisher.none.fl_str_mv |
Pergamon-elsevier Science Ltd |
| dc.source.none.fl_str_mv |
reponame:CONICET Digital (CONICET) instname:Consejo Nacional de Investigaciones Científicas y Técnicas |
| reponame_str |
CONICET Digital (CONICET) |
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CONICET Digital (CONICET) |
| instname_str |
Consejo Nacional de Investigaciones Científicas y Técnicas |
| repository.name.fl_str_mv |
CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicas |
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dasensio@conicet.gov.ar; lcarlino@conicet.gov.ar |
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1846083190042656768 |
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13.22299 |