Estudo de equilíbrio líquido-vapor de soluções hidroetanólicas contendo frutose

Detalhes bibliográficos
Ano de defesa: 2016
Autor(a) principal: Dias, Rafael Macedo
Orientador(a): Badino Júnior, Alberto Colli lattes
Banca de defesa: Não Informado pela instituição
Tipo de documento: Dissertação
Tipo de acesso: Acesso aberto
Idioma: por
Instituição de defesa: Universidade Federal de São Carlos
Câmpus São Carlos
Programa de Pós-Graduação: Programa de Pós-Graduação em Engenharia Química - PPGEQ
Departamento: Não Informado pela instituição
País: Não Informado pela instituição
Palavras-chave em Português:
Palavras-chave em Inglês:
Área do conhecimento CNPq:
Link de acesso: https://repositorio.ufscar.br/handle/20.500.14289/10900
Resumo: Fructose (1,3,4,5,6-pentahydroxyhex-2-one) is an important sugar in global market because its unique characteristics when compared to another sugars. It becomes the fructose economically attractive besides the fact that it is not easily produced. Fructose may be produced by crystallization from its aqueous solution adding ethanol as antisolvent, and afterward a separation process will be necessary to separate ethanol+water+fructose to become the process practicable. Applying this way, ethanol may be recovered using a distillation column and vaporliquid equilibrium data for water+ethanol+fructose mixture are necessary but it is not available in literature yet. Thermodynamic models are necessary to modelate a distillation column. Thus, this work has the objective of obtain VLE of hydroethanolic solutions contain fructose, and estimate parameters of an adequated model to describe the behavior of the mixture. In this work, Vapor-liquid equilibrium (VLE) data for water+ethanol+fructose and water+ethanol were determined using a modified ebulliometer based on vapor recirculation operating at atmospheric pressure of São Carlos. The composition was determinated combinating measures of refractive index and mass balance. Curves of VLE with fix composition of fructose containing 10.3%, 20.7% and 31.0% in mass were determinated, besides a binary curve with water and ethanol to validate the method. The estimative of parameters was realized in Scilab software version 5.5.1, utilizing the Levenberg-Marquardt method. The experimental data were used to estimate parameters of models based on excess Gibbs energy and local composition (Wilson, NRTL, UNIQUAC, P&M-UNIQUAC). Among all the model tested on estimative of parameters, the best model to describe the experimental data was the P&M-UNIQUAC model whose parameters were considered dependents of temperature with maximum deviation of 6,10% to water in vapor phase. Were evaluated models based on modifications of UNIFAC model, in these cases using parameters of interaction available in literature, to these cases the best model to describe the experimental was the mS-UNIFAC with maximum deviation of 14,45% to water in vapor phase. The results show that is possible determinate VLE data contain fructose utilizing the methology adopted and that fructose influences in VLE.
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spelling Dias, Rafael MacedoBadino Júnior, Alberto Collihttp://lattes.cnpq.br/6244428434217018Bernardo, Andréhttp://lattes.cnpq.br/5705402824877708http://lattes.cnpq.br/49078081832664338db50ba3-6c3d-41a4-85b5-788bd869695a2019-02-04T18:57:46Z2019-02-04T18:57:46Z2016-02-15DIAS, Rafael Macedo. Estudo de equilíbrio líquido-vapor de soluções hidroetanólicas contendo frutose. 2016. Dissertação (Mestrado em Engenharia Química) – Universidade Federal de São Carlos, São Carlos, 2016. Disponível em: https://repositorio.ufscar.br/handle/20.500.14289/10900.https://repositorio.ufscar.br/handle/20.500.14289/10900Fructose (1,3,4,5,6-pentahydroxyhex-2-one) is an important sugar in global market because its unique characteristics when compared to another sugars. It becomes the fructose economically attractive besides the fact that it is not easily produced. Fructose may be produced by crystallization from its aqueous solution adding ethanol as antisolvent, and afterward a separation process will be necessary to separate ethanol+water+fructose to become the process practicable. Applying this way, ethanol may be recovered using a distillation column and vaporliquid equilibrium data for water+ethanol+fructose mixture are necessary but it is not available in literature yet. Thermodynamic models are necessary to modelate a distillation column. Thus, this work has the objective of obtain VLE of hydroethanolic solutions contain fructose, and estimate parameters of an adequated model to describe the behavior of the mixture. In this work, Vapor-liquid equilibrium (VLE) data for water+ethanol+fructose and water+ethanol were determined using a modified ebulliometer based on vapor recirculation operating at atmospheric pressure of São Carlos. The composition was determinated combinating measures of refractive index and mass balance. Curves of VLE with fix composition of fructose containing 10.3%, 20.7% and 31.0% in mass were determinated, besides a binary curve with water and ethanol to validate the method. The estimative of parameters was realized in Scilab software version 5.5.1, utilizing the Levenberg-Marquardt method. The experimental data were used to estimate parameters of models based on excess Gibbs energy and local composition (Wilson, NRTL, UNIQUAC, P&M-UNIQUAC). Among all the model tested on estimative of parameters, the best model to describe the experimental data was the P&M-UNIQUAC model whose parameters were considered dependents of temperature with maximum deviation of 6,10% to water in vapor phase. Were evaluated models based on modifications of UNIFAC model, in these cases using parameters of interaction available in literature, to these cases the best model to describe the experimental was the mS-UNIFAC with maximum deviation of 14,45% to water in vapor phase. The results show that is possible determinate VLE data contain fructose utilizing the methology adopted and that fructose influences in VLE.A frutose é um monossacarídeo muito importante no mercado mundial, apresentando características diferenciadas quando comparado aos demais açúcares, o que a torna economicamente atrativa embora não sendo produzida em grande escala no Brasil. Um dos métodos possíveis para produzi-la seria utilizar etanol como antissolvente após a hidrólise da sacarose, para facilitar a cristalização da frutose no meio e separá-la em seguida. Utilizando essa via, a recuperação de etanol se faz necessária em de uma coluna de destilação, e para isso, dados de equilíbrio líquido-vapor (ELV) são importantes para analisar a viabilidade do processo, mas que não se encontram na literatura ainda. Modelos termodinâmicos se fazem necessários para uma futura modelagem da coluna de destilação. Em vista disso, o presente trabalho tem como objetivo obter dados de ELV da solução hidroetanólica contendo frutose, e estimar parâmetros de um modelo adequado para descrição do comportamento de tal mistura. A obtenção dos dados de ELV foi realizada utilizando um ebuliômetro modificado com recirculação da fase vapor operando à pressão atmosférica da cidade de São Carlos-SP. A composição foi determinada por balanço de massa combinado com medidas de índice de refração. Foram feitas curvas de ELV com composição fixa de frutose de 10,3%, 20,7% e 31,0% em massa, além de uma curva binária de etanol e água para validar o método. A estimativa de parâmetros de interação foi realizada no software Scilab versão 5.5.1 através do método de Levenberg-Marquardt. Os dados experimentais foram utilizados para ajustar parâmetros de modelos de energia de Gibbs excedente baseados em composição local (Wilson, NRTL, UNIQUAC, e P&M-UNIQUAC). Dentre todos os modelos testados nos ajustes de parâmetros, o melhor modelo para a descrição dos dados foi o modelo P&M-UNIQUAC cujos parâmetros foram considerados dependentes da temperatura com um desvio máximo de 6,10% para a água na fase vapor. Foram avaliados também modelos baseados em modificação do modelo UNIFAC, nesses casos utilizando os parâmetros de interação da literatura, para os quais o melhor modelo na descrição dos dados experimentais foi o mS-UNIFAC com desvio máximo de 14,45% para a água na fase vapor. Os resultados mostraram que é possível determinar dados de ELV contendo frutose utilizando a metodologia adotada e que a frutose influência no ELV.Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)porUniversidade Federal de São CarlosCâmpus São CarlosPrograma de Pós-Graduação em Engenharia Química - PPGEQUFSCarEquilíbrio líquido-vaporFrutoseEbuliômetroAjuste de parâmetros bináriosLiquid-vapor equilibriumFructoseEbulliometerEstimative of parametersENGENHARIAS::ENGENHARIA QUIMICAEstudo de equilíbrio líquido-vapor de soluções hidroetanólicas contendo frutoseinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/masterThesisOnline60060029d76c9b-aac3-4e11-bdb2-5988dc628937info:eu-repo/semantics/openAccessreponame:Repositório Institucional da UFSCARinstname:Universidade Federal de São Carlos (UFSCAR)instacron:UFSCARORIGINALDissRMD.pdfDissRMD.pdfapplication/pdf3005669https://repositorio.ufscar.br/bitstreams/77f334c3-da39-4946-ad89-969024545987/downloadc09a70c69f5277d78ad50e546bf5f9e4MD51trueAnonymousREADLICENSElicense.txtlicense.txttext/plain; charset=utf-81957https://repositorio.ufscar.br/bitstreams/41dcb2a9-f9ae-4948-86e4-5a7cf199ad2c/downloadae0398b6f8b235e40ad82cba6c50031dMD52falseAnonymousREADTEXTDissRMD.pdf.txtDissRMD.pdf.txtExtracted texttext/plain247620https://repositorio.ufscar.br/bitstreams/cd65a446-9416-4881-9ae6-780efaff04a7/download42a7c7a4c09b56246e13f3022efdcd2cMD55falseAnonymousREADTHUMBNAILDissRMD.pdf.jpgDissRMD.pdf.jpgIM Thumbnailimage/jpeg4328https://repositorio.ufscar.br/bitstreams/736e893e-fa6d-4973-9dd4-f60105e0edb3/download67d307ae2a1e858429d23cbbb750439fMD56falseAnonymousREAD20.500.14289/109002025-02-05 18:04:20.715Acesso abertoopen.accessoai:repositorio.ufscar.br:20.500.14289/10900https://repositorio.ufscar.brRepositório InstitucionalPUBhttps://repositorio.ufscar.br/oai/requestrepositorio.sibi@ufscar.bropendoar:43222025-02-05T21:04:20Repositório Institucional da UFSCAR - Universidade Federal de São Carlos (UFSCAR)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
dc.title.por.fl_str_mv Estudo de equilíbrio líquido-vapor de soluções hidroetanólicas contendo frutose
title Estudo de equilíbrio líquido-vapor de soluções hidroetanólicas contendo frutose
spellingShingle Estudo de equilíbrio líquido-vapor de soluções hidroetanólicas contendo frutose
Dias, Rafael Macedo
Equilíbrio líquido-vapor
Frutose
Ebuliômetro
Ajuste de parâmetros binários
Liquid-vapor equilibrium
Fructose
Ebulliometer
Estimative of parameters
ENGENHARIAS::ENGENHARIA QUIMICA
title_short Estudo de equilíbrio líquido-vapor de soluções hidroetanólicas contendo frutose
title_full Estudo de equilíbrio líquido-vapor de soluções hidroetanólicas contendo frutose
title_fullStr Estudo de equilíbrio líquido-vapor de soluções hidroetanólicas contendo frutose
title_full_unstemmed Estudo de equilíbrio líquido-vapor de soluções hidroetanólicas contendo frutose
title_sort Estudo de equilíbrio líquido-vapor de soluções hidroetanólicas contendo frutose
author Dias, Rafael Macedo
author_facet Dias, Rafael Macedo
author_role author
dc.contributor.authorlattes.por.fl_str_mv http://lattes.cnpq.br/4907808183266433
dc.contributor.author.fl_str_mv Dias, Rafael Macedo
dc.contributor.advisor1.fl_str_mv Badino Júnior, Alberto Colli
dc.contributor.advisor1Lattes.fl_str_mv http://lattes.cnpq.br/6244428434217018
dc.contributor.advisor-co1.fl_str_mv Bernardo, André
dc.contributor.advisor-co1Lattes.fl_str_mv http://lattes.cnpq.br/5705402824877708
dc.contributor.authorID.fl_str_mv 8db50ba3-6c3d-41a4-85b5-788bd869695a
contributor_str_mv Badino Júnior, Alberto Colli
Bernardo, André
dc.subject.por.fl_str_mv Equilíbrio líquido-vapor
Frutose
Ebuliômetro
Ajuste de parâmetros binários
topic Equilíbrio líquido-vapor
Frutose
Ebuliômetro
Ajuste de parâmetros binários
Liquid-vapor equilibrium
Fructose
Ebulliometer
Estimative of parameters
ENGENHARIAS::ENGENHARIA QUIMICA
dc.subject.eng.fl_str_mv Liquid-vapor equilibrium
Fructose
Ebulliometer
Estimative of parameters
dc.subject.cnpq.fl_str_mv ENGENHARIAS::ENGENHARIA QUIMICA
description Fructose (1,3,4,5,6-pentahydroxyhex-2-one) is an important sugar in global market because its unique characteristics when compared to another sugars. It becomes the fructose economically attractive besides the fact that it is not easily produced. Fructose may be produced by crystallization from its aqueous solution adding ethanol as antisolvent, and afterward a separation process will be necessary to separate ethanol+water+fructose to become the process practicable. Applying this way, ethanol may be recovered using a distillation column and vaporliquid equilibrium data for water+ethanol+fructose mixture are necessary but it is not available in literature yet. Thermodynamic models are necessary to modelate a distillation column. Thus, this work has the objective of obtain VLE of hydroethanolic solutions contain fructose, and estimate parameters of an adequated model to describe the behavior of the mixture. In this work, Vapor-liquid equilibrium (VLE) data for water+ethanol+fructose and water+ethanol were determined using a modified ebulliometer based on vapor recirculation operating at atmospheric pressure of São Carlos. The composition was determinated combinating measures of refractive index and mass balance. Curves of VLE with fix composition of fructose containing 10.3%, 20.7% and 31.0% in mass were determinated, besides a binary curve with water and ethanol to validate the method. The estimative of parameters was realized in Scilab software version 5.5.1, utilizing the Levenberg-Marquardt method. The experimental data were used to estimate parameters of models based on excess Gibbs energy and local composition (Wilson, NRTL, UNIQUAC, P&M-UNIQUAC). Among all the model tested on estimative of parameters, the best model to describe the experimental data was the P&M-UNIQUAC model whose parameters were considered dependents of temperature with maximum deviation of 6,10% to water in vapor phase. Were evaluated models based on modifications of UNIFAC model, in these cases using parameters of interaction available in literature, to these cases the best model to describe the experimental was the mS-UNIFAC with maximum deviation of 14,45% to water in vapor phase. The results show that is possible determinate VLE data contain fructose utilizing the methology adopted and that fructose influences in VLE.
publishDate 2016
dc.date.issued.fl_str_mv 2016-02-15
dc.date.accessioned.fl_str_mv 2019-02-04T18:57:46Z
dc.date.available.fl_str_mv 2019-02-04T18:57:46Z
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 DIAS, Rafael Macedo. Estudo de equilíbrio líquido-vapor de soluções hidroetanólicas contendo frutose. 2016. Dissertação (Mestrado em Engenharia Química) – Universidade Federal de São Carlos, São Carlos, 2016. Disponível em: https://repositorio.ufscar.br/handle/20.500.14289/10900.
dc.identifier.uri.fl_str_mv https://repositorio.ufscar.br/handle/20.500.14289/10900
identifier_str_mv DIAS, Rafael Macedo. Estudo de equilíbrio líquido-vapor de soluções hidroetanólicas contendo frutose. 2016. Dissertação (Mestrado em Engenharia Química) – Universidade Federal de São Carlos, São Carlos, 2016. Disponível em: https://repositorio.ufscar.br/handle/20.500.14289/10900.
url https://repositorio.ufscar.br/handle/20.500.14289/10900
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dc.publisher.none.fl_str_mv Universidade Federal de São Carlos
Câmpus São Carlos
dc.publisher.program.fl_str_mv Programa de Pós-Graduação em Engenharia Química - PPGEQ
dc.publisher.initials.fl_str_mv UFSCar
publisher.none.fl_str_mv Universidade Federal de São Carlos
Câmpus São Carlos
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