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dc.contributor.authorKoch, Reinhold
dc.contributor.authorLópez, Eduardo
dc.contributor.authorJiménez Divins, Nuria
dc.contributor.authorAllué Fantova, Miguel
dc.contributor.authorJossen, Andreas
dc.contributor.authorRiera, Jordi (Riera Colomer)
dc.contributor.authorLlorca Piqué, Jordi
dc.contributor.otherUniversitat Politècnica de Catalunya. Institut de Tècniques Energètiques
dc.contributor.otherUniversitat Politècnica de Catalunya. Departament d'Enginyeria de Sistemes, Automàtica i Informàtica Industrial
dc.date.accessioned2013-05-31T09:26:20Z
dc.date.created2013
dc.date.issued2013
dc.identifier.citationKoch, R. [et al.]. Ethanol catalytic membrane reformer for direct PEM FC feeding. "International journal of hydrogen energy", 2013, vol. 38, núm. 14, p. 5605-5615.
dc.identifier.issn0360-3199
dc.identifier.urihttp://hdl.handle.net/2117/19469
dc.description.abstractIn 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, ethanol–water 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.
dc.format.extent11 p.
dc.language.isoeng
dc.rightsAttribution-NonCommercial-NoDerivs 3.0 Spain
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/3.0/es/
dc.subjectÀrees temàtiques de la UPC::Energies
dc.subjectÀrees temàtiques de la UPC::Enginyeria química::Indústria dels processos químics
dc.subject.lcshEthanol as fuel
dc.subject.lcshCatalytic reforming
dc.titleEthanol catalytic membrane reformer for direct PEM FC feeding
dc.typeArticle
dc.subject.lemacHidrògen com a combustible
dc.contributor.groupUniversitat Politècnica de Catalunya. ACES - Control Avançat de Sistemes d'Energia
dc.contributor.groupUniversitat Politècnica de Catalunya. GREENER - Grup de recerca d'estudis energètics i de les radiacions
dc.identifier.doi10.1016/j.ijhydene.2013.02.107
dc.relation.publisherversionhttp://dx.doi.org/10.1016/j.ijhydene.2013.02.107
dc.rights.accessRestricted access - publisher's policy
local.identifier.drac12438313
dc.description.versionPostprint (published version)
dc.date.lift10000-01-01
local.citation.authorKoch, R.; López, E.; Jimenez, N.; Allué, M.; Jossen, A.; Riera, J.; Llorca, J.
local.citation.publicationNameInternational journal of hydrogen energy
local.citation.volume38
local.citation.number14
local.citation.startingPage5605
local.citation.endingPage5615


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Attribution-NonCommercial-NoDerivs 3.0 Spain
Except where otherwise noted, content on this work is licensed under a Creative Commons license : Attribution-NonCommercial-NoDerivs 3.0 Spain