Avaliação da interesterificação catalítica de óleo de macaúba com acetato de metila

Detalhes bibliográficos
Autor(a) principal: Ribeiro, Jéssica dos Santos
Data de Publicação: 2017
Tipo de documento: Dissertação
Idioma: por
Título da fonte: Manancial - Repositório Digital da UFSM
Texto Completo: http://repositorio.ufsm.br/handle/1/12929
Resumo: The world concern about the increasing of energy demand, depletion of fossil fuel reserves and global warming aroused interest in biodiesel production. Commonly produced through basic homogeneous transesterification, the increase in biodiesel production resulted in an overproduction of glycerol. Thus, the aim of this study was to promote and evaluate interesterification reaction of macaw oil with methyl acetate over different heterogeneous catalysts (γ-alumina, zeolite HY, niobium phosphate and niobic acid), for production of fatty acid methyl esters (FAME) and triacetin, compound with high added value, considered an additive to biodiesel, instead of glycerol. The catalyst γ-alumina presented superior results when the reaction conditions were 250 °C, 5% mass of catalyst and molar ratio methyl acetate to oil of 30:1 and in 1 hour of reaction it was reached 54.07% (w/w) of FAME and triacetin content. At these conditions the catalyst was recovered and reused without treatment for at least 5 cycles without significant catalytic activity loss. Also, the influence of temperature (225 °C to 300 °C), catalyst mass (2 to 10% of oil mass fed) and methyl acetate to oil molar ratio (10:1 to 40:1) were evaluated. FAME and triacetin content of 48.96% (w/w) and 1.84% (w/w) were achieved for 300 °C, 2% of γ-alumina and molar ratio of 20:1, in 1 hour of reaction which corresponds to 82.5% of conversion considering the convertibility of macaw oil to esters and triacetin of 61.6% (w/w). The catalyst was recovered and reused without treatment for at least 4 cycles and did not present significant catalytic activity loss.
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spelling Avaliação da interesterificação catalítica de óleo de macaúba com acetato de metilaEvaluation of catalytic interesterification of macaw oil with methyl acetateBiodieselTriacetinaCatálise heterogêneaAluminaNióbioBiodieselTriacetinHeterogeneous catalysisAluminaNiobiumCNPQ::ENGENHARIAS::ENGENHARIA QUIMICAThe world concern about the increasing of energy demand, depletion of fossil fuel reserves and global warming aroused interest in biodiesel production. Commonly produced through basic homogeneous transesterification, the increase in biodiesel production resulted in an overproduction of glycerol. Thus, the aim of this study was to promote and evaluate interesterification reaction of macaw oil with methyl acetate over different heterogeneous catalysts (γ-alumina, zeolite HY, niobium phosphate and niobic acid), for production of fatty acid methyl esters (FAME) and triacetin, compound with high added value, considered an additive to biodiesel, instead of glycerol. The catalyst γ-alumina presented superior results when the reaction conditions were 250 °C, 5% mass of catalyst and molar ratio methyl acetate to oil of 30:1 and in 1 hour of reaction it was reached 54.07% (w/w) of FAME and triacetin content. At these conditions the catalyst was recovered and reused without treatment for at least 5 cycles without significant catalytic activity loss. Also, the influence of temperature (225 °C to 300 °C), catalyst mass (2 to 10% of oil mass fed) and methyl acetate to oil molar ratio (10:1 to 40:1) were evaluated. FAME and triacetin content of 48.96% (w/w) and 1.84% (w/w) were achieved for 300 °C, 2% of γ-alumina and molar ratio of 20:1, in 1 hour of reaction which corresponds to 82.5% of conversion considering the convertibility of macaw oil to esters and triacetin of 61.6% (w/w). The catalyst was recovered and reused without treatment for at least 4 cycles and did not present significant catalytic activity loss.Coordenação de Aperfeiçoamento de Pessoal de Nível Superior - CAPESA preocupação mundial com o aumento da demanda de energia, o esgotamento das reservas de combustíveis fósseis e o aquecimento global despertaram interesse na produção de biodiesel. Geralmente produzido por transesterificação homogênea básica, o aumento na produção de biodiesel resultou em uma superprodução de glicerol. Assim, o objetivo deste estudo foi promover e avaliar a reação de interesterificação do óleo de macaúba com acetato de metila sobre diferentes catalisadores heterogêneos (γ-alumina, zeólita HY, fosfato de nióbio e ácido nióbico), para a produção de ésteres metílicos de ácidos graxos (EMAGs) e triacetina, composto com alto valor agregado, considerado um aditivo ao biodiesel, ao contrário do glicerol. O catalisador γ-alumina apresentou resultados superiores quando as condições de reação foram de 250 ° C, 5% de massa de catalisador e razão molar de acetato de metila para óleo de 30: 1 e, em 1 hora de reação, foram obtidos de 54,07% de teor (m/m) de EMAG e de triacetina. Nestas condições, o catalisador foi recuperado e reutilizado sem tratamento pelo menos 5 ciclos sem perda significativa de atividade catalítica. Também foram avaliadas a influência da temperatura (225 ° C a 300 ° C), da massa de catalisador (2 a 10% da massa de óleo alimentada) e da razão molar de acetato de metila para óleo (10: 1 a 40: 1). Foram obtidos valores de EMAGs e triacetina de 48,96% (m/m) e 1,84% (m/m) para 300 ° C, 2% de γ-alumina e razão molar de 20:1, em 1 hora de reação, o que corresponde a 82,5% de conversão considerando a conversibilidade do óleo de macaúba a ésteres e triacetina de 61,6% (m/m). O catalisador foi recuperado e reutilizado sem tratamento pelo menos 4 ciclos e não apresentou significativa perda de atividade catalítica.Universidade Federal de Santa MariaBrasilEngenharia QuímicaUFSMPrograma de Pós-Graduação em Engenharia QuímicaCentro de TecnologiaCastilhos, Fernanda dehttp://lattes.cnpq.br/4590978604104577Muniz, Ana Rosa Costahttp://lattes.cnpq.br/6878938083195939Salau, Nina Paula Gonçalveshttp://lattes.cnpq.br/4234840503539989Ribeiro, Jéssica dos Santos2018-04-11T14:41:49Z2018-04-11T14:41:49Z2017-01-27info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/masterThesisapplication/pdfhttp://repositorio.ufsm.br/handle/1/12929porAttribution-NonCommercial-NoDerivatives 4.0 Internationalhttp://creativecommons.org/licenses/by-nc-nd/4.0/info:eu-repo/semantics/openAccessreponame:Manancial - Repositório Digital da UFSMinstname:Universidade Federal de Santa Maria (UFSM)instacron:UFSM2018-04-11T14:41:50Zoai:repositorio.ufsm.br:1/12929Biblioteca Digital de Teses e Dissertaçõeshttps://repositorio.ufsm.br/ONGhttps://repositorio.ufsm.br/oai/requestatendimento.sib@ufsm.br||tedebc@gmail.comopendoar:2018-04-11T14:41:50Manancial - Repositório Digital da UFSM - Universidade Federal de Santa Maria (UFSM)false
dc.title.none.fl_str_mv Avaliação da interesterificação catalítica de óleo de macaúba com acetato de metila
Evaluation of catalytic interesterification of macaw oil with methyl acetate
title Avaliação da interesterificação catalítica de óleo de macaúba com acetato de metila
spellingShingle Avaliação da interesterificação catalítica de óleo de macaúba com acetato de metila
Ribeiro, Jéssica dos Santos
Biodiesel
Triacetina
Catálise heterogênea
Alumina
Nióbio
Biodiesel
Triacetin
Heterogeneous catalysis
Alumina
Niobium
CNPQ::ENGENHARIAS::ENGENHARIA QUIMICA
title_short Avaliação da interesterificação catalítica de óleo de macaúba com acetato de metila
title_full Avaliação da interesterificação catalítica de óleo de macaúba com acetato de metila
title_fullStr Avaliação da interesterificação catalítica de óleo de macaúba com acetato de metila
title_full_unstemmed Avaliação da interesterificação catalítica de óleo de macaúba com acetato de metila
title_sort Avaliação da interesterificação catalítica de óleo de macaúba com acetato de metila
author Ribeiro, Jéssica dos Santos
author_facet Ribeiro, Jéssica dos Santos
author_role author
dc.contributor.none.fl_str_mv Castilhos, Fernanda de
http://lattes.cnpq.br/4590978604104577
Muniz, Ana Rosa Costa
http://lattes.cnpq.br/6878938083195939
Salau, Nina Paula Gonçalves
http://lattes.cnpq.br/4234840503539989
dc.contributor.author.fl_str_mv Ribeiro, Jéssica dos Santos
dc.subject.por.fl_str_mv Biodiesel
Triacetina
Catálise heterogênea
Alumina
Nióbio
Biodiesel
Triacetin
Heterogeneous catalysis
Alumina
Niobium
CNPQ::ENGENHARIAS::ENGENHARIA QUIMICA
topic Biodiesel
Triacetina
Catálise heterogênea
Alumina
Nióbio
Biodiesel
Triacetin
Heterogeneous catalysis
Alumina
Niobium
CNPQ::ENGENHARIAS::ENGENHARIA QUIMICA
description The world concern about the increasing of energy demand, depletion of fossil fuel reserves and global warming aroused interest in biodiesel production. Commonly produced through basic homogeneous transesterification, the increase in biodiesel production resulted in an overproduction of glycerol. Thus, the aim of this study was to promote and evaluate interesterification reaction of macaw oil with methyl acetate over different heterogeneous catalysts (γ-alumina, zeolite HY, niobium phosphate and niobic acid), for production of fatty acid methyl esters (FAME) and triacetin, compound with high added value, considered an additive to biodiesel, instead of glycerol. The catalyst γ-alumina presented superior results when the reaction conditions were 250 °C, 5% mass of catalyst and molar ratio methyl acetate to oil of 30:1 and in 1 hour of reaction it was reached 54.07% (w/w) of FAME and triacetin content. At these conditions the catalyst was recovered and reused without treatment for at least 5 cycles without significant catalytic activity loss. Also, the influence of temperature (225 °C to 300 °C), catalyst mass (2 to 10% of oil mass fed) and methyl acetate to oil molar ratio (10:1 to 40:1) were evaluated. FAME and triacetin content of 48.96% (w/w) and 1.84% (w/w) were achieved for 300 °C, 2% of γ-alumina and molar ratio of 20:1, in 1 hour of reaction which corresponds to 82.5% of conversion considering the convertibility of macaw oil to esters and triacetin of 61.6% (w/w). The catalyst was recovered and reused without treatment for at least 4 cycles and did not present significant catalytic activity loss.
publishDate 2017
dc.date.none.fl_str_mv 2017-01-27
2018-04-11T14:41:49Z
2018-04-11T14:41:49Z
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
dc.type.driver.fl_str_mv info:eu-repo/semantics/masterThesis
format masterThesis
status_str publishedVersion
dc.identifier.uri.fl_str_mv http://repositorio.ufsm.br/handle/1/12929
url http://repositorio.ufsm.br/handle/1/12929
dc.language.iso.fl_str_mv por
language por
dc.rights.driver.fl_str_mv Attribution-NonCommercial-NoDerivatives 4.0 International
http://creativecommons.org/licenses/by-nc-nd/4.0/
info:eu-repo/semantics/openAccess
rights_invalid_str_mv Attribution-NonCommercial-NoDerivatives 4.0 International
http://creativecommons.org/licenses/by-nc-nd/4.0/
eu_rights_str_mv openAccess
dc.format.none.fl_str_mv application/pdf
dc.publisher.none.fl_str_mv Universidade Federal de Santa Maria
Brasil
Engenharia Química
UFSM
Programa de Pós-Graduação em Engenharia Química
Centro de Tecnologia
publisher.none.fl_str_mv Universidade Federal de Santa Maria
Brasil
Engenharia Química
UFSM
Programa de Pós-Graduação em Engenharia Química
Centro de Tecnologia
dc.source.none.fl_str_mv reponame:Manancial - Repositório Digital da UFSM
instname:Universidade Federal de Santa Maria (UFSM)
instacron:UFSM
instname_str Universidade Federal de Santa Maria (UFSM)
instacron_str UFSM
institution UFSM
reponame_str Manancial - Repositório Digital da UFSM
collection Manancial - Repositório Digital da UFSM
repository.name.fl_str_mv Manancial - Repositório Digital da UFSM - Universidade Federal de Santa Maria (UFSM)
repository.mail.fl_str_mv atendimento.sib@ufsm.br||tedebc@gmail.com
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