Dynamic analysis of an ethanol steam reformer for hydrogen production
Autor(a) principal: | |
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Data de Publicação: | 2018 |
Outros Autores: | , , |
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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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) |
repository.mail.fl_str_mv |
|
_version_ |
1808128783004205056 |