Dynamic Analysis of an Ethanol Steam Reformer for Hydrogen Production

Detalhes bibliográficos
Autor(a) principal: Llerena Pizarro, Omar R.
Data de Publicação: 2017
Outros Autores: Ocampo-Martinez, Carlos, Serra Prat, Maria, Silveira, Jose Luz [UNESP], Patino, D., Yime, E.
Tipo de documento: Artigo de conferência
Idioma: eng
Título da fonte: Repositório Institucional da UNESP
Texto Completo: http://hdl.handle.net/11449/163988
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.project DEOCS from the Spanish Ministry of Economy and CompetitivenessSENESCYTUniversidad Politecnica SalesianaUPS, Lab Mech Engn, Cuenca, EcuadorUPC, CSIC, Inst Robot & Informat Ind, Barcelona, SpainSao Paulo State Univ UNESP, Dept Energy, Guaratingueta, BrazilSao Paulo State Univ UNESP, Dept Energy, Guaratingueta, Brazilproject DEOCS from the Spanish Ministry of Economy and Competitiveness: DPI2016-76493-C3-3-RIeeeUPSUPCUniversidade Estadual Paulista (Unesp)Llerena Pizarro, Omar R.Ocampo-Martinez, CarlosSerra Prat, MariaSilveira, Jose Luz [UNESP]Patino, D.Yime, E.2018-11-26T17:48:40Z2018-11-26T17:48:40Z2017-01-01info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/conferenceObject52017 Ieee 3rd Colombian Conference On Automatic Control (ccac). New York: Ieee, 5 p., 2017.http://hdl.handle.net/11449/163988WOS:000427290700110Web of Sciencereponame:Repositório Institucional da UNESPinstname:Universidade Estadual Paulista (UNESP)instacron:UNESPeng2017 Ieee 3rd Colombian Conference On Automatic Control (ccac)info:eu-repo/semantics/openAccess2021-10-23T21:44:37Zoai:repositorio.unesp.br:11449/163988Repositório InstitucionalPUBhttp://repositorio.unesp.br/oai/requestopendoar:29462021-10-23T21:44:37Repositório 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
Llerena Pizarro, Omar R.
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 Llerena Pizarro, Omar R.
author_facet Llerena Pizarro, Omar R.
Ocampo-Martinez, Carlos
Serra Prat, Maria
Silveira, Jose Luz [UNESP]
Patino, D.
Yime, E.
author_role author
author2 Ocampo-Martinez, Carlos
Serra Prat, Maria
Silveira, Jose Luz [UNESP]
Patino, D.
Yime, E.
author2_role author
author
author
author
author
dc.contributor.none.fl_str_mv UPS
UPC
Universidade Estadual Paulista (Unesp)
dc.contributor.author.fl_str_mv Llerena Pizarro, Omar R.
Ocampo-Martinez, Carlos
Serra Prat, Maria
Silveira, Jose Luz [UNESP]
Patino, D.
Yime, E.
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 2017
dc.date.none.fl_str_mv 2017-01-01
2018-11-26T17:48:40Z
2018-11-26T17:48:40Z
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
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dc.identifier.uri.fl_str_mv 2017 Ieee 3rd Colombian Conference On Automatic Control (ccac). New York: Ieee, 5 p., 2017.
http://hdl.handle.net/11449/163988
WOS:000427290700110
identifier_str_mv 2017 Ieee 3rd Colombian Conference On Automatic Control (ccac). New York: Ieee, 5 p., 2017.
WOS:000427290700110
url http://hdl.handle.net/11449/163988
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instname:Universidade Estadual Paulista (UNESP)
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