Study of solvents alternative for aromatic extraction

Detalhes bibliográficos
Autor(a) principal: Francisca Maria Rodrigues Mesquita
Data de Publicação: 2015
Tipo de documento: Tese
Idioma: por
Título da fonte: Biblioteca Digital de Teses e Dissertações da UFC
Texto Completo: http://www.teses.ufc.br/tde_busca/arquivo.php?codArquivo=14637
Resumo: Aromatic hydrocarbons are chemical compounds of great interest in the petrochemical industry. These are commonly derived from reformed naphtha, which are in multicomponent mixtures with aliphatic hydrocarbons. The separation of these components is realized, generally, the liquid-liquid extraction process. In this process, the sulfolane is the most widely used solvent. However, this has some disadvantages such as high cost. For this reason, many studies are developed by the academic community in order to propose alternative solvents to replace the exclusive use of sulfolane by compounds that are important features like good selectivity, easy recoverability and low costs. Given the above, this study main aims to determine liquid-liquid equilibrium data (LLE) to study the ability of solvents [diethylene glycol (DEG), triethylene glycol (TEG), glycerol and 2-hydroxyethyl amine format (2-HEAF)] in extracting aromatic mixtures with aliphatic. The physical properties also of great importance in the understanding of the behavior and interactions that occur in liquid mixtures. Thus, in this study were also studied the density and viscosity of solvent extractors aromatic. The experimental methodology for the determination of LLE data was initially validated by reproducing the literature, and the results showed good agreement between these data. After the method has been validated, solubility curves and tie-lines were constructed for systems containing decane + toluene + DEG (+ TEG, + glycerol, + 2-HEAF, + sulfolane) at T = (303.15 and 333.15) K. The composition data of tie-lines, obtained experimentally, were used to calculate the selectivity parameter and the distribution coefficient. With this data, it can be concluded that all the solvents studied have a good capacity for toluene extraction from mixtures with decane. However, the glycerol has presented as the most promising solvent for aromatics extraction. Finally, the experimental data were correlated through the thermodynamic activity coefficient models, NRTL and UNIQUAC. The results were considered satisfactory, noting that the NRTL was the model that presented minor deviations in compositions. Thus, best represented the LLE data for the systems studied.
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spelling info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/doctoralThesisStudy of solvents alternative for aromatic extractionEstudo de solventes alternativos para extraÃÃo de aromÃticos2015-04-24RÃlvia Saraiva de Santiago Aguiar83900098387Hosiberto Batista de Sant'Ana55184820434Fabiano Andrà Narciso Fernandes26059059856http://lattes.cnpq.br/9978219072711522Izabelly Larissa Lucena65070720368Geormenny Rocha dos Santos39981410225http://lattes.cnpq.br/08446626019456690010636730http://lattes.cnpq.br/0384846482774966Francisca Maria Rodrigues MesquitaUniversidade Federal do CearÃPrograma de PÃs-GraduaÃÃo em Engenharia QuÃmicaUFCBRDecano Tolueno Solventes alternativos EquilÃbrio lÃquido-lÃquido Modelagem termodinÃmicaCompostos aromÃticosDecane Toluene Alternatives Solvents Liquid-Liquid Equilibria Thermodynamic modeling.TERMODINAMICAAromatic hydrocarbons are chemical compounds of great interest in the petrochemical industry. These are commonly derived from reformed naphtha, which are in multicomponent mixtures with aliphatic hydrocarbons. The separation of these components is realized, generally, the liquid-liquid extraction process. In this process, the sulfolane is the most widely used solvent. However, this has some disadvantages such as high cost. For this reason, many studies are developed by the academic community in order to propose alternative solvents to replace the exclusive use of sulfolane by compounds that are important features like good selectivity, easy recoverability and low costs. Given the above, this study main aims to determine liquid-liquid equilibrium data (LLE) to study the ability of solvents [diethylene glycol (DEG), triethylene glycol (TEG), glycerol and 2-hydroxyethyl amine format (2-HEAF)] in extracting aromatic mixtures with aliphatic. The physical properties also of great importance in the understanding of the behavior and interactions that occur in liquid mixtures. Thus, in this study were also studied the density and viscosity of solvent extractors aromatic. The experimental methodology for the determination of LLE data was initially validated by reproducing the literature, and the results showed good agreement between these data. After the method has been validated, solubility curves and tie-lines were constructed for systems containing decane + toluene + DEG (+ TEG, + glycerol, + 2-HEAF, + sulfolane) at T = (303.15 and 333.15) K. The composition data of tie-lines, obtained experimentally, were used to calculate the selectivity parameter and the distribution coefficient. With this data, it can be concluded that all the solvents studied have a good capacity for toluene extraction from mixtures with decane. However, the glycerol has presented as the most promising solvent for aromatics extraction. Finally, the experimental data were correlated through the thermodynamic activity coefficient models, NRTL and UNIQUAC. The results were considered satisfactory, noting that the NRTL was the model that presented minor deviations in compositions. Thus, best represented the LLE data for the systems studied. Os hidrocarbonetos aromÃticos sÃo compostos quÃmicos de grande interesse na indÃstria petroquÃmica. Estes sÃo comumente originados da nafta reformada, onde encontram-se em misturas multicomponentes com hidrocarbonetos alifÃticos. A separaÃÃo destes componentes à realizada, em sua grande maioria, pelo processo de extraÃÃo lÃquido-lÃquido. Nesse processo, o sulfolano à o solvente mais utilizado. No entanto, este apresenta algumas desvantagens, tais como alto custo. Por esse motivo, inÃmeros estudos sÃo realizados pela comunidade acadÃmica a fim de propor solventes alternativos que substituam o uso exclusivo do sulfolano por compostos que tambÃm apresentem caracterÃsticas importantes, como boa seletividade, boa recuperabilidade e baixos custos. Diante do exposto, o presente trabalho tem como principal objetivo determinar dados de equilÃbrio lÃquido-lÃquido (ELL) para estudar a capacidade dos solventes [dietilenoglicol (DEG), trietilenoglicol (TEG), glicerina e 2-hidroxietilamina formato (2-HEAF)] em extrair aromÃticos das misturas com alifÃticos. As propriedades fÃsicas tambÃm assumem extrema importÃncia no conhecimento do comportamento e das interaÃÃes que ocorrem nas misturas de lÃquidos. Deste modo, neste trabalho foram estudados a densidade e a viscosidade de solventes extratores de aromÃticos. A metodologia experimental para obtenÃÃo dos dados de ELL foi inicialmente validada reproduzindo dados da literatura, e os resultados mostraram uma boa concordÃncia entre estes dados. ApÃs a metodologia ter sido validada foram construÃdas curvas de solubilidade e tie-lines para os sistemas contendo decano + tolueno + DEG (+ TEG, + glicerina, + 2-HEAF, + sulfolano) a T = (303,15 e 333,15) K. Os dados de composiÃÃo das tie-lines, obtidos experimentalmente, foram utilizados para calcular o parÃmetro de seletividade e o coeficiente de distribuiÃÃo. De posse desses dados, pode-se concluir que todos os solventes estudados apresentam boa capacidade para extraÃÃo de tolueno a partir de misturas com decano. No entanto, a glicerina destacou-se como o solvente mais promissor para a extraÃÃo de aromÃticos apresentando os maiores valores para seletividade. Finalmente, os dados experimentais foram correlacionados atravÃs dos modelos termodinÃmicos de coeficiente de atividade, NRTL e UNIQUAC. Os resultados foram considerados satisfatÃrios, observando-se que o NRTL foi o modelo que apresentou os menores desvios na composiÃÃo. Dessa forma, representou melhor os dados de ELL para os sistemas estudados. CoordenaÃÃo de AperfeÃoamento de Pessoal de NÃvel Superior http://www.teses.ufc.br/tde_busca/arquivo.php?codArquivo=14637application/pdfinfo:eu-repo/semantics/openAccessporreponame:Biblioteca Digital de Teses e Dissertações da UFCinstname:Universidade Federal do Cearáinstacron:UFC2019-01-21T11:27:58Zmail@mail.com -
dc.title.en.fl_str_mv Study of solvents alternative for aromatic extraction
dc.title.alternative.pt.fl_str_mv Estudo de solventes alternativos para extraÃÃo de aromÃticos
title Study of solvents alternative for aromatic extraction
spellingShingle Study of solvents alternative for aromatic extraction
Francisca Maria Rodrigues Mesquita
Decano
Tolueno
Solventes alternativos
EquilÃbrio lÃquido-lÃquido
Modelagem termodinÃmica
Compostos aromÃticos
Decane
Toluene
Alternatives Solvents
Liquid-Liquid Equilibria
Thermodynamic modeling.
TERMODINAMICA
title_short Study of solvents alternative for aromatic extraction
title_full Study of solvents alternative for aromatic extraction
title_fullStr Study of solvents alternative for aromatic extraction
title_full_unstemmed Study of solvents alternative for aromatic extraction
title_sort Study of solvents alternative for aromatic extraction
author Francisca Maria Rodrigues Mesquita
author_facet Francisca Maria Rodrigues Mesquita
author_role author
dc.contributor.advisor1.fl_str_mv RÃlvia Saraiva de Santiago Aguiar
dc.contributor.advisor1ID.fl_str_mv 83900098387
dc.contributor.advisor-co1.fl_str_mv Hosiberto Batista de Sant'Ana
dc.contributor.advisor-co1ID.fl_str_mv 55184820434
dc.contributor.referee1.fl_str_mv Fabiano Andrà Narciso Fernandes
dc.contributor.referee1ID.fl_str_mv 26059059856
dc.contributor.referee1Lattes.fl_str_mv http://lattes.cnpq.br/9978219072711522
dc.contributor.referee2.fl_str_mv Izabelly Larissa Lucena
dc.contributor.referee2ID.fl_str_mv 65070720368
dc.contributor.referee3.fl_str_mv Geormenny Rocha dos Santos
dc.contributor.referee3ID.fl_str_mv 39981410225
dc.contributor.referee3Lattes.fl_str_mv http://lattes.cnpq.br/0844662601945669
dc.contributor.authorID.fl_str_mv 0010636730
dc.contributor.authorLattes.fl_str_mv http://lattes.cnpq.br/0384846482774966
dc.contributor.author.fl_str_mv Francisca Maria Rodrigues Mesquita
contributor_str_mv RÃlvia Saraiva de Santiago Aguiar
Hosiberto Batista de Sant'Ana
Fabiano Andrà Narciso Fernandes
Izabelly Larissa Lucena
Geormenny Rocha dos Santos
dc.subject.por.fl_str_mv Decano
Tolueno
Solventes alternativos
EquilÃbrio lÃquido-lÃquido
Modelagem termodinÃmica
Compostos aromÃticos
topic Decano
Tolueno
Solventes alternativos
EquilÃbrio lÃquido-lÃquido
Modelagem termodinÃmica
Compostos aromÃticos
Decane
Toluene
Alternatives Solvents
Liquid-Liquid Equilibria
Thermodynamic modeling.
TERMODINAMICA
dc.subject.eng.fl_str_mv Decane
Toluene
Alternatives Solvents
Liquid-Liquid Equilibria
Thermodynamic modeling.
dc.subject.cnpq.fl_str_mv TERMODINAMICA
dc.description.sponsorship.fl_txt_mv CoordenaÃÃo de AperfeÃoamento de Pessoal de NÃvel Superior
dc.description.abstract.por.fl_txt_mv Aromatic hydrocarbons are chemical compounds of great interest in the petrochemical industry. These are commonly derived from reformed naphtha, which are in multicomponent mixtures with aliphatic hydrocarbons. The separation of these components is realized, generally, the liquid-liquid extraction process. In this process, the sulfolane is the most widely used solvent. However, this has some disadvantages such as high cost. For this reason, many studies are developed by the academic community in order to propose alternative solvents to replace the exclusive use of sulfolane by compounds that are important features like good selectivity, easy recoverability and low costs. Given the above, this study main aims to determine liquid-liquid equilibrium data (LLE) to study the ability of solvents [diethylene glycol (DEG), triethylene glycol (TEG), glycerol and 2-hydroxyethyl amine format (2-HEAF)] in extracting aromatic mixtures with aliphatic. The physical properties also of great importance in the understanding of the behavior and interactions that occur in liquid mixtures. Thus, in this study were also studied the density and viscosity of solvent extractors aromatic. The experimental methodology for the determination of LLE data was initially validated by reproducing the literature, and the results showed good agreement between these data. After the method has been validated, solubility curves and tie-lines were constructed for systems containing decane + toluene + DEG (+ TEG, + glycerol, + 2-HEAF, + sulfolane) at T = (303.15 and 333.15) K. The composition data of tie-lines, obtained experimentally, were used to calculate the selectivity parameter and the distribution coefficient. With this data, it can be concluded that all the solvents studied have a good capacity for toluene extraction from mixtures with decane. However, the glycerol has presented as the most promising solvent for aromatics extraction. Finally, the experimental data were correlated through the thermodynamic activity coefficient models, NRTL and UNIQUAC. The results were considered satisfactory, noting that the NRTL was the model that presented minor deviations in compositions. Thus, best represented the LLE data for the systems studied.
Os hidrocarbonetos aromÃticos sÃo compostos quÃmicos de grande interesse na indÃstria petroquÃmica. Estes sÃo comumente originados da nafta reformada, onde encontram-se em misturas multicomponentes com hidrocarbonetos alifÃticos. A separaÃÃo destes componentes à realizada, em sua grande maioria, pelo processo de extraÃÃo lÃquido-lÃquido. Nesse processo, o sulfolano à o solvente mais utilizado. No entanto, este apresenta algumas desvantagens, tais como alto custo. Por esse motivo, inÃmeros estudos sÃo realizados pela comunidade acadÃmica a fim de propor solventes alternativos que substituam o uso exclusivo do sulfolano por compostos que tambÃm apresentem caracterÃsticas importantes, como boa seletividade, boa recuperabilidade e baixos custos. Diante do exposto, o presente trabalho tem como principal objetivo determinar dados de equilÃbrio lÃquido-lÃquido (ELL) para estudar a capacidade dos solventes [dietilenoglicol (DEG), trietilenoglicol (TEG), glicerina e 2-hidroxietilamina formato (2-HEAF)] em extrair aromÃticos das misturas com alifÃticos. As propriedades fÃsicas tambÃm assumem extrema importÃncia no conhecimento do comportamento e das interaÃÃes que ocorrem nas misturas de lÃquidos. Deste modo, neste trabalho foram estudados a densidade e a viscosidade de solventes extratores de aromÃticos. A metodologia experimental para obtenÃÃo dos dados de ELL foi inicialmente validada reproduzindo dados da literatura, e os resultados mostraram uma boa concordÃncia entre estes dados. ApÃs a metodologia ter sido validada foram construÃdas curvas de solubilidade e tie-lines para os sistemas contendo decano + tolueno + DEG (+ TEG, + glicerina, + 2-HEAF, + sulfolano) a T = (303,15 e 333,15) K. Os dados de composiÃÃo das tie-lines, obtidos experimentalmente, foram utilizados para calcular o parÃmetro de seletividade e o coeficiente de distribuiÃÃo. De posse desses dados, pode-se concluir que todos os solventes estudados apresentam boa capacidade para extraÃÃo de tolueno a partir de misturas com decano. No entanto, a glicerina destacou-se como o solvente mais promissor para a extraÃÃo de aromÃticos apresentando os maiores valores para seletividade. Finalmente, os dados experimentais foram correlacionados atravÃs dos modelos termodinÃmicos de coeficiente de atividade, NRTL e UNIQUAC. Os resultados foram considerados satisfatÃrios, observando-se que o NRTL foi o modelo que apresentou os menores desvios na composiÃÃo. Dessa forma, representou melhor os dados de ELL para os sistemas estudados.
description Aromatic hydrocarbons are chemical compounds of great interest in the petrochemical industry. These are commonly derived from reformed naphtha, which are in multicomponent mixtures with aliphatic hydrocarbons. The separation of these components is realized, generally, the liquid-liquid extraction process. In this process, the sulfolane is the most widely used solvent. However, this has some disadvantages such as high cost. For this reason, many studies are developed by the academic community in order to propose alternative solvents to replace the exclusive use of sulfolane by compounds that are important features like good selectivity, easy recoverability and low costs. Given the above, this study main aims to determine liquid-liquid equilibrium data (LLE) to study the ability of solvents [diethylene glycol (DEG), triethylene glycol (TEG), glycerol and 2-hydroxyethyl amine format (2-HEAF)] in extracting aromatic mixtures with aliphatic. The physical properties also of great importance in the understanding of the behavior and interactions that occur in liquid mixtures. Thus, in this study were also studied the density and viscosity of solvent extractors aromatic. The experimental methodology for the determination of LLE data was initially validated by reproducing the literature, and the results showed good agreement between these data. After the method has been validated, solubility curves and tie-lines were constructed for systems containing decane + toluene + DEG (+ TEG, + glycerol, + 2-HEAF, + sulfolane) at T = (303.15 and 333.15) K. The composition data of tie-lines, obtained experimentally, were used to calculate the selectivity parameter and the distribution coefficient. With this data, it can be concluded that all the solvents studied have a good capacity for toluene extraction from mixtures with decane. However, the glycerol has presented as the most promising solvent for aromatics extraction. Finally, the experimental data were correlated through the thermodynamic activity coefficient models, NRTL and UNIQUAC. The results were considered satisfactory, noting that the NRTL was the model that presented minor deviations in compositions. Thus, best represented the LLE data for the systems studied.
publishDate 2015
dc.date.issued.fl_str_mv 2015-04-24
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