Análise termodinâmica da reforma com vapor de água de um composto modelo de bio-óleo para produção de hidrogênio

Detalhes bibliográficos
Autor(a) principal: Trevisan, Ivo Junior
Data de Publicação: 2018
Tipo de documento: Dissertação
Idioma: por
Título da fonte: Repositório Institucional da UFG
Texto Completo: http://repositorio.bc.ufg.br/tede/handle/tede/9187
Resumo: In this work, a thermodynamic analysis of the water vapor reforming reaction of a bio-oil model compound was performed and the objective is producing hydrogen through an alternative source of fossil fuels. The bio-oil model compound was considered to be a molar fraction of 1:1:1 mixture of phenol, acetic acid and hydroxyketone and the thermodynamic data were obtained in DIPPR® software version 1.2.0. The chemical and phase equilibrium were calculated by the Gibbs energy minimization method. Constant pressure of 1 bar, temperature ratio from 673.15K to 1273.15K and water and carbon ratio of the substrate (H2O(v)/C(ent)) of 0.01 to 3.00 were used to construct the optimization problem and the software GAMS® version 2.0.29.8 was used by optimization problem resolution. The gas phase was considered with behavior of ideal gas and the solid phase was considered with solid carbon. Hydrogen, water, carbon monoxide, carbon dioxide, solid carbon and methane formation data were collected after solving the optimization problem and the reaction heat and syngas production were also analyzed. The maximum hydrogen yield obtained was 1.3 moles in the 1100 K region with 1 mole water per carbon of the substrate (H2O(v)/C(ent)). It was also observed that the greater amount of syngas occurs in the 950 K region and 1,2 of the H2O(v)/C(ent) ratio. An exothermic region and an exothermic region were observed in the reaction heat analysis and in the exothermic region there is a higher incidence of coke and methane generation and in the endothermic region a higher incidence of hydrogen and carbon monoxide generation.
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spelling Souza, Thiago Leandro dehttp://buscatextual.cnpq.br/buscatextual/visualizacv.do?metodo=apresentar&id=K4250090T1Alonso, Cristian Gonçalveshttp://buscatextual.cnpq.br/buscatextual/visualizacv.do?metodo=apresentar&id=K4777466U2Souza, Thiago Leandro deAlonso , Cristian GonçalvesCardozo Filho, LucioOliveira, Sérgio Botelho deOstroski , Índianara Conceiçãohttp://buscatextual.cnpq.br/buscatextual/visualizacv.do?id=K4278312J6Trevisan, Ivo Junior2018-12-26T11:41:32Z2018-09-28TREVISAN, I. J. Análise termodinâmica da reforma com vapor de água de um composto modelo de bio-óleo para produção de hidrogênio. 2018. 91 f. Dissertação (Mestrado em Engenharia Química) - Universidade Federal de Goiás, Goiânia, 2018.http://repositorio.bc.ufg.br/tede/handle/tede/9187In this work, a thermodynamic analysis of the water vapor reforming reaction of a bio-oil model compound was performed and the objective is producing hydrogen through an alternative source of fossil fuels. The bio-oil model compound was considered to be a molar fraction of 1:1:1 mixture of phenol, acetic acid and hydroxyketone and the thermodynamic data were obtained in DIPPR® software version 1.2.0. The chemical and phase equilibrium were calculated by the Gibbs energy minimization method. Constant pressure of 1 bar, temperature ratio from 673.15K to 1273.15K and water and carbon ratio of the substrate (H2O(v)/C(ent)) of 0.01 to 3.00 were used to construct the optimization problem and the software GAMS® version 2.0.29.8 was used by optimization problem resolution. The gas phase was considered with behavior of ideal gas and the solid phase was considered with solid carbon. Hydrogen, water, carbon monoxide, carbon dioxide, solid carbon and methane formation data were collected after solving the optimization problem and the reaction heat and syngas production were also analyzed. The maximum hydrogen yield obtained was 1.3 moles in the 1100 K region with 1 mole water per carbon of the substrate (H2O(v)/C(ent)). It was also observed that the greater amount of syngas occurs in the 950 K region and 1,2 of the H2O(v)/C(ent) ratio. An exothermic region and an exothermic region were observed in the reaction heat analysis and in the exothermic region there is a higher incidence of coke and methane generation and in the endothermic region a higher incidence of hydrogen and carbon monoxide generation.Neste trabalho foi realizada uma análise termodinâmica da reação de reforma com vapor de água de um composto modelo do bio-óleo com o objetivo de produzir hidrogênio por meio de uma fonte alternativa aos combustíveis fósseis. O composto modelo do bio-óleo foi considerado como sendo uma mistura de fenol, ácido acético e hidroxicetona na proporção molar de 1:1:1 e os dados termodinâmicos utilizados foram obtidos no software DIPPR® versão 1.2.0. O equilíbrio químico e de fases foram calculados pelo método de minimização de energia de Gibbs. Pressão constante de 1 bar, temperatura de 673,15K a 1273,15K e proporção de água e carbono do substrato (H2O(v)/C(ent)) de 0,01 a 3,00 foram utilizados para a construção do problema de otimizaçãoe o software GAMS® versão 2.0.29.8para resolução. A fase gasosa foi considerada com comportamento de gás ideal e a fase sólida foi considerada com carbono sólido. Dados da formação de hidrogênio, água, monóxido de carbono, dióxido de carbono, carbono sólido e metano foram coletados após a resolução do problema de otimização e o calor de reação e a produção de syngás também foram analisados. A produção máxima de hidrogênio obtida foi de 1,3 moles na região de 1100 K com 1 mol de água por carbono do substrato (H2O(v)/C(ent)). Observou-se também que a maior quantidade de syngás acontece na região 950K e 1,2 da razão H2O(v)/C(ent). Umaregião endotérmica e uma região exotérmica foram observadas na análise do calor de reação, sendo que na região exotérmica há maior incidência da geração de coque e metano e na região endotérmica maior incidência da geração de hidrogênio e monóxido de carbono.Submitted by Marlene Santos (marlene.bc.ufg@gmail.com) on 2018-12-21T19:36:01Z No. of bitstreams: 2 Dissertação - Ivo Junior Trevisan - 2018.pdf: 3203798 bytes, checksum: 3932d86134647030491efbb4d535ac86 (MD5) license_rdf: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5)Approved for entry into archive by Luciana Ferreira (lucgeral@gmail.com) on 2018-12-26T11:41:32Z (GMT) No. of bitstreams: 2 Dissertação - Ivo Junior Trevisan - 2018.pdf: 3203798 bytes, checksum: 3932d86134647030491efbb4d535ac86 (MD5) license_rdf: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5)Made available in DSpace on 2018-12-26T11:41:32Z (GMT). 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dc.title.eng.fl_str_mv Análise termodinâmica da reforma com vapor de água de um composto modelo de bio-óleo para produção de hidrogênio
dc.title.alternative.eng.fl_str_mv Thermodynamic analysis of steam reforming reaction of bio-oil model compound to hydrogen production
title Análise termodinâmica da reforma com vapor de água de um composto modelo de bio-óleo para produção de hidrogênio
spellingShingle Análise termodinâmica da reforma com vapor de água de um composto modelo de bio-óleo para produção de hidrogênio
Trevisan, Ivo Junior
Reforma com vapor de água
Bio-óleo
Análise termodinâmica
Minimização de Gibbs
Steam reforming
Bio-oil
Thermodynamicanalysis
Gibbsminimization
CIENCIAS EXATAS E DA TERRA::QUIMICA
title_short Análise termodinâmica da reforma com vapor de água de um composto modelo de bio-óleo para produção de hidrogênio
title_full Análise termodinâmica da reforma com vapor de água de um composto modelo de bio-óleo para produção de hidrogênio
title_fullStr Análise termodinâmica da reforma com vapor de água de um composto modelo de bio-óleo para produção de hidrogênio
title_full_unstemmed Análise termodinâmica da reforma com vapor de água de um composto modelo de bio-óleo para produção de hidrogênio
title_sort Análise termodinâmica da reforma com vapor de água de um composto modelo de bio-óleo para produção de hidrogênio
author Trevisan, Ivo Junior
author_facet Trevisan, Ivo Junior
author_role author
dc.contributor.advisor1.fl_str_mv Souza, Thiago Leandro de
dc.contributor.advisor1Lattes.fl_str_mv http://buscatextual.cnpq.br/buscatextual/visualizacv.do?metodo=apresentar&id=K4250090T1
dc.contributor.advisor-co1.fl_str_mv Alonso, Cristian Gonçalves
dc.contributor.advisor-co1Lattes.fl_str_mv http://buscatextual.cnpq.br/buscatextual/visualizacv.do?metodo=apresentar&id=K4777466U2
dc.contributor.referee1.fl_str_mv Souza, Thiago Leandro de
dc.contributor.referee2.fl_str_mv Alonso , Cristian Gonçalves
dc.contributor.referee3.fl_str_mv Cardozo Filho, Lucio
dc.contributor.referee4.fl_str_mv Oliveira, Sérgio Botelho de
dc.contributor.referee5.fl_str_mv Ostroski , Índianara Conceição
dc.contributor.authorLattes.fl_str_mv http://buscatextual.cnpq.br/buscatextual/visualizacv.do?id=K4278312J6
dc.contributor.author.fl_str_mv Trevisan, Ivo Junior
contributor_str_mv Souza, Thiago Leandro de
Alonso, Cristian Gonçalves
Souza, Thiago Leandro de
Alonso , Cristian Gonçalves
Cardozo Filho, Lucio
Oliveira, Sérgio Botelho de
Ostroski , Índianara Conceição
dc.subject.por.fl_str_mv Reforma com vapor de água
Bio-óleo
Análise termodinâmica
Minimização de Gibbs
topic Reforma com vapor de água
Bio-óleo
Análise termodinâmica
Minimização de Gibbs
Steam reforming
Bio-oil
Thermodynamicanalysis
Gibbsminimization
CIENCIAS EXATAS E DA TERRA::QUIMICA
dc.subject.eng.fl_str_mv Steam reforming
Bio-oil
Thermodynamicanalysis
Gibbsminimization
dc.subject.cnpq.fl_str_mv CIENCIAS EXATAS E DA TERRA::QUIMICA
description In this work, a thermodynamic analysis of the water vapor reforming reaction of a bio-oil model compound was performed and the objective is producing hydrogen through an alternative source of fossil fuels. The bio-oil model compound was considered to be a molar fraction of 1:1:1 mixture of phenol, acetic acid and hydroxyketone and the thermodynamic data were obtained in DIPPR® software version 1.2.0. The chemical and phase equilibrium were calculated by the Gibbs energy minimization method. Constant pressure of 1 bar, temperature ratio from 673.15K to 1273.15K and water and carbon ratio of the substrate (H2O(v)/C(ent)) of 0.01 to 3.00 were used to construct the optimization problem and the software GAMS® version 2.0.29.8 was used by optimization problem resolution. The gas phase was considered with behavior of ideal gas and the solid phase was considered with solid carbon. Hydrogen, water, carbon monoxide, carbon dioxide, solid carbon and methane formation data were collected after solving the optimization problem and the reaction heat and syngas production were also analyzed. The maximum hydrogen yield obtained was 1.3 moles in the 1100 K region with 1 mole water per carbon of the substrate (H2O(v)/C(ent)). It was also observed that the greater amount of syngas occurs in the 950 K region and 1,2 of the H2O(v)/C(ent) ratio. An exothermic region and an exothermic region were observed in the reaction heat analysis and in the exothermic region there is a higher incidence of coke and methane generation and in the endothermic region a higher incidence of hydrogen and carbon monoxide generation.
publishDate 2018
dc.date.accessioned.fl_str_mv 2018-12-26T11:41:32Z
dc.date.issued.fl_str_mv 2018-09-28
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
dc.type.driver.fl_str_mv info:eu-repo/semantics/masterThesis
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status_str publishedVersion
dc.identifier.citation.fl_str_mv TREVISAN, I. J. Análise termodinâmica da reforma com vapor de água de um composto modelo de bio-óleo para produção de hidrogênio. 2018. 91 f. Dissertação (Mestrado em Engenharia Química) - Universidade Federal de Goiás, Goiânia, 2018.
dc.identifier.uri.fl_str_mv http://repositorio.bc.ufg.br/tede/handle/tede/9187
identifier_str_mv TREVISAN, I. J. Análise termodinâmica da reforma com vapor de água de um composto modelo de bio-óleo para produção de hidrogênio. 2018. 91 f. Dissertação (Mestrado em Engenharia Química) - Universidade Federal de Goiás, Goiânia, 2018.
url http://repositorio.bc.ufg.br/tede/handle/tede/9187
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language por
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dc.publisher.none.fl_str_mv Universidade Federal de Goiás
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dc.publisher.initials.fl_str_mv UFG
dc.publisher.country.fl_str_mv Brasil
dc.publisher.department.fl_str_mv Instituto de Química - IQ (RG)
publisher.none.fl_str_mv Universidade Federal de Goiás
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