Dynamic analysis of an ethanol steam reformer for hydrogen production

Detalhes bibliográficos
Autor(a) principal: Pizarro, Omar R. Llerena
Data de Publicação: 2018
Outros Autores: Ocampo-Martinez, Carlos, Prat, Maria Serra, Silveira, Jose Luz [UNESP]
Tipo de documento: Artigo de conferência
Idioma: eng
Título da fonte: Repositório Institucional da UNESP
Texto Completo: http://dx.doi.org/10.1109/CCAC.2017.8276488
http://hdl.handle.net/11449/179885
Resumo: The attempt to improve hydrogen quality has motivated research focused solely on the design of reactors for hydrogen production, paying little interest to their modelling and much less attention to its dynamic analysis. For these main reasons, this paper is focused on the dynamic analysis of a mathematical model of an ethanol steam reformer (ESR) for producing hydrogen. This analysis differs from other nonlinear analyses since it is applied to a specific seventh-order system, while literature presents analyses for at most fourth-order systems. The nonlinear model used is based on mass balances. It is represented by partial differential equations (PDEs), which are converted into ordinary differential equations (ODEs) by the finite-differences method over the space. A general nonlinear dynamic analysis based on equilibrium points and their local stability is carried out by using these ODEs. Dynamic analysis results show that the studied reactor has a stable equilibrium point for a physical-sense range of inputs (ethanol + water), which allow to have available key criteria for the design of control strategies.
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spelling Dynamic analysis of an ethanol steam reformer for hydrogen productionThe attempt to improve hydrogen quality has motivated research focused solely on the design of reactors for hydrogen production, paying little interest to their modelling and much less attention to its dynamic analysis. For these main reasons, this paper is focused on the dynamic analysis of a mathematical model of an ethanol steam reformer (ESR) for producing hydrogen. This analysis differs from other nonlinear analyses since it is applied to a specific seventh-order system, while literature presents analyses for at most fourth-order systems. The nonlinear model used is based on mass balances. It is represented by partial differential equations (PDEs), which are converted into ordinary differential equations (ODEs) by the finite-differences method over the space. A general nonlinear dynamic analysis based on equilibrium points and their local stability is carried out by using these ODEs. Dynamic analysis results show that the studied reactor has a stable equilibrium point for a physical-sense range of inputs (ethanol + water), which allow to have available key criteria for the design of control strategies.Secretaría de Educación Superior, Ciencia, Tecnología e InnovaciónLaboratory of Mechanical Engineering Universidad Politécnica Salesiana (UPS)Universitat Politècnica de Catalunya Institut de Robòtica i Informàtica Industrial (CSIC-UPC)Department of Energy Sao Paulo State University (UNESP)Department of Energy Sao Paulo State University (UNESP)Universidad Politécnica Salesiana (UPS)Institut de Robòtica i Informàtica Industrial (CSIC-UPC)Universidade Estadual Paulista (Unesp)Pizarro, Omar R. LlerenaOcampo-Martinez, CarlosPrat, Maria SerraSilveira, Jose Luz [UNESP]2018-12-11T17:37:09Z2018-12-11T17:37:09Z2018-01-30info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/conferenceObject1-5http://dx.doi.org/10.1109/CCAC.2017.82764882017 IEEE 3rd Colombian Conference on Automatic Control, CCAC 2017 - Conference Proceedings, v. 2018-January, p. 1-5.http://hdl.handle.net/11449/17988510.1109/CCAC.2017.82764882-s2.0-85047304711Scopusreponame:Repositório Institucional da UNESPinstname:Universidade Estadual Paulista (UNESP)instacron:UNESPeng2017 IEEE 3rd Colombian Conference on Automatic Control, CCAC 2017 - Conference Proceedingsinfo:eu-repo/semantics/openAccess2024-07-01T19:30:12Zoai:repositorio.unesp.br:11449/179885Repositório InstitucionalPUBhttp://repositorio.unesp.br/oai/requestopendoar:29462024-08-05T17:16:38.755370Repositório Institucional da UNESP - Universidade Estadual Paulista (UNESP)false
dc.title.none.fl_str_mv Dynamic analysis of an ethanol steam reformer for hydrogen production
title Dynamic analysis of an ethanol steam reformer for hydrogen production
spellingShingle Dynamic analysis of an ethanol steam reformer for hydrogen production
Pizarro, Omar R. Llerena
title_short Dynamic analysis of an ethanol steam reformer for hydrogen production
title_full Dynamic analysis of an ethanol steam reformer for hydrogen production
title_fullStr Dynamic analysis of an ethanol steam reformer for hydrogen production
title_full_unstemmed Dynamic analysis of an ethanol steam reformer for hydrogen production
title_sort Dynamic analysis of an ethanol steam reformer for hydrogen production
author Pizarro, Omar R. Llerena
author_facet Pizarro, Omar R. Llerena
Ocampo-Martinez, Carlos
Prat, Maria Serra
Silveira, Jose Luz [UNESP]
author_role author
author2 Ocampo-Martinez, Carlos
Prat, Maria Serra
Silveira, Jose Luz [UNESP]
author2_role author
author
author
dc.contributor.none.fl_str_mv Universidad Politécnica Salesiana (UPS)
Institut de Robòtica i Informàtica Industrial (CSIC-UPC)
Universidade Estadual Paulista (Unesp)
dc.contributor.author.fl_str_mv Pizarro, Omar R. Llerena
Ocampo-Martinez, Carlos
Prat, Maria Serra
Silveira, Jose Luz [UNESP]
description The attempt to improve hydrogen quality has motivated research focused solely on the design of reactors for hydrogen production, paying little interest to their modelling and much less attention to its dynamic analysis. For these main reasons, this paper is focused on the dynamic analysis of a mathematical model of an ethanol steam reformer (ESR) for producing hydrogen. This analysis differs from other nonlinear analyses since it is applied to a specific seventh-order system, while literature presents analyses for at most fourth-order systems. The nonlinear model used is based on mass balances. It is represented by partial differential equations (PDEs), which are converted into ordinary differential equations (ODEs) by the finite-differences method over the space. A general nonlinear dynamic analysis based on equilibrium points and their local stability is carried out by using these ODEs. Dynamic analysis results show that the studied reactor has a stable equilibrium point for a physical-sense range of inputs (ethanol + water), which allow to have available key criteria for the design of control strategies.
publishDate 2018
dc.date.none.fl_str_mv 2018-12-11T17:37:09Z
2018-12-11T17:37:09Z
2018-01-30
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
dc.type.driver.fl_str_mv info:eu-repo/semantics/conferenceObject
format conferenceObject
status_str publishedVersion
dc.identifier.uri.fl_str_mv http://dx.doi.org/10.1109/CCAC.2017.8276488
2017 IEEE 3rd Colombian Conference on Automatic Control, CCAC 2017 - Conference Proceedings, v. 2018-January, p. 1-5.
http://hdl.handle.net/11449/179885
10.1109/CCAC.2017.8276488
2-s2.0-85047304711
url http://dx.doi.org/10.1109/CCAC.2017.8276488
http://hdl.handle.net/11449/179885
identifier_str_mv 2017 IEEE 3rd Colombian Conference on Automatic Control, CCAC 2017 - Conference Proceedings, v. 2018-January, p. 1-5.
10.1109/CCAC.2017.8276488
2-s2.0-85047304711
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv 2017 IEEE 3rd Colombian Conference on Automatic Control, CCAC 2017 - Conference Proceedings
dc.rights.driver.fl_str_mv info:eu-repo/semantics/openAccess
eu_rights_str_mv openAccess
dc.format.none.fl_str_mv 1-5
dc.source.none.fl_str_mv Scopus
reponame:Repositório Institucional da UNESP
instname:Universidade Estadual Paulista (UNESP)
instacron:UNESP
instname_str Universidade Estadual Paulista (UNESP)
instacron_str UNESP
institution UNESP
reponame_str Repositório Institucional da UNESP
collection Repositório Institucional da UNESP
repository.name.fl_str_mv Repositório Institucional da UNESP - Universidade Estadual Paulista (UNESP)
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