Thermoeconomic analysis of hydrogen incorporation in a biodiesel plant

Detalhes bibliográficos
Autor(a) principal: Boloy, Ronney Arismel Mancebo [UNESP]
Data de Publicação: 2017
Outros Autores: Silva, Marcio Evaristo [UNESP], Valle, Atilio Erazo [UNESP], Silveira, José Luz [UNESP], Tuna, Celso Eduardo [UNESP]
Tipo de documento: Artigo
Idioma: eng
Título da fonte: Repositório Institucional da UNESP
Texto Completo: http://dx.doi.org/10.1016/j.applthermaleng.2016.10.171
http://hdl.handle.net/11449/173817
Resumo: The paper develops a methodology that uses the thermoeconomic functional diagram applied for allocating cost of products obtained by the plant and afterwards demonstrates how it is possible to calculate the marginal cost in US$/kW h of the production. The methodology which was adopted includes the plant exergetic analysis development, the function system identification through physical diagram of the plant, construction of the Thermoeconomic Functional Diagram and the determination of the expressions for the plant's exergetic functions. The methodology also includes the determination of some parameters such as, investments, maintenance, operation, raw materials (canola oil, catalysts, methanol, glycerine and natural gas) and utility costs (electricity and steam water). As a result, it can be said that the simultaneously production of biodiesel and hydrogen is a suitable technology to minimize biodiesel production cost. About 6% of the thermoeconomic cost of biodiesel production was diminished when compared to the values previously published in the present literature. In relation to the hydrogen production thermoeconomic costs, the values are closer when they are compared to the ones which were identified in the literature. As a contribution to the scientific knowledge, it can be said that the obtained results shows the high performance of simultaneous biodiesel and hydrogen production, especially when glycerine is further processed into valuable energetic matter, in other words, considering economic aspects associated with the exergy conception, in order to develop a tool to assist the equipment operation, as well as to optimize the biodiesel plant design. Also shows that in a biodiesel production plant the hydrogen technology is more sustainable than the traditional one. The paper aims to innovate the production process of biodiesel by incorporating the hydrogen production process through glycerine steam reforming.
id UNSP_1b329cccb24e611d6b9890a3556a38e6
oai_identifier_str oai:repositorio.unesp.br:11449/173817
network_acronym_str UNSP
network_name_str Repositório Institucional da UNESP
repository_id_str 2946
spelling Thermoeconomic analysis of hydrogen incorporation in a biodiesel plantBiodieselCostFunctional diagramGlycerineHydrogenThermoeconomicThe paper develops a methodology that uses the thermoeconomic functional diagram applied for allocating cost of products obtained by the plant and afterwards demonstrates how it is possible to calculate the marginal cost in US$/kW h of the production. The methodology which was adopted includes the plant exergetic analysis development, the function system identification through physical diagram of the plant, construction of the Thermoeconomic Functional Diagram and the determination of the expressions for the plant's exergetic functions. The methodology also includes the determination of some parameters such as, investments, maintenance, operation, raw materials (canola oil, catalysts, methanol, glycerine and natural gas) and utility costs (electricity and steam water). As a result, it can be said that the simultaneously production of biodiesel and hydrogen is a suitable technology to minimize biodiesel production cost. About 6% of the thermoeconomic cost of biodiesel production was diminished when compared to the values previously published in the present literature. In relation to the hydrogen production thermoeconomic costs, the values are closer when they are compared to the ones which were identified in the literature. As a contribution to the scientific knowledge, it can be said that the obtained results shows the high performance of simultaneous biodiesel and hydrogen production, especially when glycerine is further processed into valuable energetic matter, in other words, considering economic aspects associated with the exergy conception, in order to develop a tool to assist the equipment operation, as well as to optimize the biodiesel plant design. Also shows that in a biodiesel production plant the hydrogen technology is more sustainable than the traditional one. The paper aims to innovate the production process of biodiesel by incorporating the hydrogen production process through glycerine steam reforming.Group of Entrepreneurship Energy Environment and Technology Mechanical Engineering Department Technological and Education Federal CenterOptimization and Energetic Systems Group (GOSE) Department of Energy College of Engineering at Guaratinguetá São Paulo State University (UNESP), Av Dr. Ariberto Pereira da Cunha, 333, Pedregulho, GuaratinguetáOptimization and Energetic Systems Group (GOSE) Department of Energy College of Engineering at Guaratinguetá São Paulo State University (UNESP), Av Dr. Ariberto Pereira da Cunha, 333, Pedregulho, GuaratinguetáTechnological and Education Federal CenterUniversidade Estadual Paulista (Unesp)Boloy, Ronney Arismel Mancebo [UNESP]Silva, Marcio Evaristo [UNESP]Valle, Atilio Erazo [UNESP]Silveira, José Luz [UNESP]Tuna, Celso Eduardo [UNESP]2018-12-11T17:07:53Z2018-12-11T17:07:53Z2017-02-25info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/article519-528application/pdfhttp://dx.doi.org/10.1016/j.applthermaleng.2016.10.171Applied Thermal Engineering, v. 113, p. 519-528.1359-4311http://hdl.handle.net/11449/17381710.1016/j.applthermaleng.2016.10.1712-s2.0-849965581292-s2.0-84996558129.pdfScopusreponame:Repositório Institucional da UNESPinstname:Universidade Estadual Paulista (UNESP)instacron:UNESPengApplied Thermal Engineering1,505info:eu-repo/semantics/openAccess2024-07-01T19:30:00Zoai:repositorio.unesp.br:11449/173817Repositório InstitucionalPUBhttp://repositorio.unesp.br/oai/requestopendoar:29462024-08-05T21:36:18.256606Repositório Institucional da UNESP - Universidade Estadual Paulista (UNESP)false
dc.title.none.fl_str_mv Thermoeconomic analysis of hydrogen incorporation in a biodiesel plant
title Thermoeconomic analysis of hydrogen incorporation in a biodiesel plant
spellingShingle Thermoeconomic analysis of hydrogen incorporation in a biodiesel plant
Boloy, Ronney Arismel Mancebo [UNESP]
Biodiesel
Cost
Functional diagram
Glycerine
Hydrogen
Thermoeconomic
title_short Thermoeconomic analysis of hydrogen incorporation in a biodiesel plant
title_full Thermoeconomic analysis of hydrogen incorporation in a biodiesel plant
title_fullStr Thermoeconomic analysis of hydrogen incorporation in a biodiesel plant
title_full_unstemmed Thermoeconomic analysis of hydrogen incorporation in a biodiesel plant
title_sort Thermoeconomic analysis of hydrogen incorporation in a biodiesel plant
author Boloy, Ronney Arismel Mancebo [UNESP]
author_facet Boloy, Ronney Arismel Mancebo [UNESP]
Silva, Marcio Evaristo [UNESP]
Valle, Atilio Erazo [UNESP]
Silveira, José Luz [UNESP]
Tuna, Celso Eduardo [UNESP]
author_role author
author2 Silva, Marcio Evaristo [UNESP]
Valle, Atilio Erazo [UNESP]
Silveira, José Luz [UNESP]
Tuna, Celso Eduardo [UNESP]
author2_role author
author
author
author
dc.contributor.none.fl_str_mv Technological and Education Federal Center
Universidade Estadual Paulista (Unesp)
dc.contributor.author.fl_str_mv Boloy, Ronney Arismel Mancebo [UNESP]
Silva, Marcio Evaristo [UNESP]
Valle, Atilio Erazo [UNESP]
Silveira, José Luz [UNESP]
Tuna, Celso Eduardo [UNESP]
dc.subject.por.fl_str_mv Biodiesel
Cost
Functional diagram
Glycerine
Hydrogen
Thermoeconomic
topic Biodiesel
Cost
Functional diagram
Glycerine
Hydrogen
Thermoeconomic
description The paper develops a methodology that uses the thermoeconomic functional diagram applied for allocating cost of products obtained by the plant and afterwards demonstrates how it is possible to calculate the marginal cost in US$/kW h of the production. The methodology which was adopted includes the plant exergetic analysis development, the function system identification through physical diagram of the plant, construction of the Thermoeconomic Functional Diagram and the determination of the expressions for the plant's exergetic functions. The methodology also includes the determination of some parameters such as, investments, maintenance, operation, raw materials (canola oil, catalysts, methanol, glycerine and natural gas) and utility costs (electricity and steam water). As a result, it can be said that the simultaneously production of biodiesel and hydrogen is a suitable technology to minimize biodiesel production cost. About 6% of the thermoeconomic cost of biodiesel production was diminished when compared to the values previously published in the present literature. In relation to the hydrogen production thermoeconomic costs, the values are closer when they are compared to the ones which were identified in the literature. As a contribution to the scientific knowledge, it can be said that the obtained results shows the high performance of simultaneous biodiesel and hydrogen production, especially when glycerine is further processed into valuable energetic matter, in other words, considering economic aspects associated with the exergy conception, in order to develop a tool to assist the equipment operation, as well as to optimize the biodiesel plant design. Also shows that in a biodiesel production plant the hydrogen technology is more sustainable than the traditional one. The paper aims to innovate the production process of biodiesel by incorporating the hydrogen production process through glycerine steam reforming.
publishDate 2017
dc.date.none.fl_str_mv 2017-02-25
2018-12-11T17:07:53Z
2018-12-11T17:07:53Z
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
dc.type.driver.fl_str_mv info:eu-repo/semantics/article
format article
status_str publishedVersion
dc.identifier.uri.fl_str_mv http://dx.doi.org/10.1016/j.applthermaleng.2016.10.171
Applied Thermal Engineering, v. 113, p. 519-528.
1359-4311
http://hdl.handle.net/11449/173817
10.1016/j.applthermaleng.2016.10.171
2-s2.0-84996558129
2-s2.0-84996558129.pdf
url http://dx.doi.org/10.1016/j.applthermaleng.2016.10.171
http://hdl.handle.net/11449/173817
identifier_str_mv Applied Thermal Engineering, v. 113, p. 519-528.
1359-4311
10.1016/j.applthermaleng.2016.10.171
2-s2.0-84996558129
2-s2.0-84996558129.pdf
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv Applied Thermal Engineering
1,505
dc.rights.driver.fl_str_mv info:eu-repo/semantics/openAccess
eu_rights_str_mv openAccess
dc.format.none.fl_str_mv 519-528
application/pdf
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_ 1808129340790013952