Transesterificação do óleo de frango empregando diferentes catalisadores

Detalhes bibliográficos
Ano de defesa: 2013
Autor(a) principal: Secco, Willian lattes
Orientador(a): Silva, Edson Antônio Alves da lattes
Banca de defesa: Bariccatti, Reinaldo Aparecido lattes, Silva, Camila da lattes
Tipo de documento: Dissertação
Tipo de acesso: Acesso aberto
Idioma: por
Instituição de defesa: Universidade Estadual do Oeste do Parana
Programa de Pós-Graduação: Programa de Pós-Graduação Stricto Sensu em Bioenergia
Departamento: Biocombustíveis
País: BR
Palavras-chave em Português:
Palavras-chave em Inglês:
Área do conhecimento CNPq:
Link de acesso: http://tede.unioeste.br:8080/tede/handle/tede/1793
Resumo: The biofuel has been assuming an incresingly important role on the environmental and economic impacts caused by fossil fuels. The biodiesel represents one of the most important biofuel in the current scenery of the expanding renewable fuels, in the energy matrix. The transesterification has prevailed as the companies, which produce this biofuel, most used process. Furthermore, the chicken oil, offal of the slaughtering industry, has good position to contribute with the expansion and diversification of biodiesel, in regions naturally vocationated by the development of the chicken slaughter industry. Moreover, this kind of oil does not compete with the food chain. The reaction of the chicken oil with short-chains alcohols using heterogeneous catalyst allow greatly the cost-cutting, by the fact that heterogeneous catalyst can be reusable in the process of the production of the biodiesel, and also because the chicken oil is an offal of low added value; the same does not occur with the homogeneous catalyst. Given this, the aim of this work was to evaluate some catalysts in the production of esters from the crude and neutral chicken oil. The following catalysts were evaluated: Amberlyst-15, Aberlite IR-120, KSF, ZnO, CaO e methanol as alcohol reagent. The preliminary reactions occurred at 60°C e 80°C, with 5% of catalyst relative to the mass of oil, time of reaction of 5 hours and molar ratio alcohol:oil of 9:1. In this conditions, the catalyst which showed higher conversions, around 77% in esters in the preliminary tests, was the calcium oxide (CaO). A pretreatment was made with the chicken oil, with the aim of improve its properties, reducing its acidity, and with that, a performance comparative outline was made between the crude oil and the neutral one. This comparision allowed the analysis of the use effect of heterogeneuous catalysts that preaches the benefits of using impure oils in biodiesel production reactions. New tests were made with the catalyst CaO by an experimental design in which 3 variables of the transesterification reaction were evaluated: temperature, molar ratio alcohol:oil, and percentage by weight of catalyst. The highest conversions were obtained in the order of 79.8% and 83% for crude and neutral oil respectively, in the conditions of 90ºC of temperature, molar ratio alcohol:oil of 6:1 and 4% in weight of catalyst. The kinetics of the reaction was also evaluated in the following conditions: temperatures of 40ºC, 60ºC and 80ºC, methanol molar ratio: 9:1 oil and 4% by weight of catalyst; in the kinetics tests were obtained conversions of up to 94.11% ester with reaction time of 24 hours. The obtained data of the best performance of the kinetics were used for the evaluation of the mathematical modeling.
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spelling Silva, Edson Antônio Alves daCPF:64656675920http://lattes.cnpq.br/9304493875700070Bariccatti, Reinaldo AparecidoCPF:08813157886http://lattes.cnpq.br/8065417966435303Silva, Camila daCPF:03335209982http://lattes.cnpq.br/0151285357488920CPF:00821580965http://lattes.cnpq.br/1737708269881791Secco, Willian2017-07-10T17:59:27Z2013-12-202013-02-08SECCO, Willian. Tranesterification oil chicken using different catalysts. 2013. 101 f. Dissertação (Mestrado em Biocombustíveis) - Universidade Estadual do Oeste do Parana, Toledo, 2013.http://tede.unioeste.br:8080/tede/handle/tede/1793The biofuel has been assuming an incresingly important role on the environmental and economic impacts caused by fossil fuels. The biodiesel represents one of the most important biofuel in the current scenery of the expanding renewable fuels, in the energy matrix. The transesterification has prevailed as the companies, which produce this biofuel, most used process. Furthermore, the chicken oil, offal of the slaughtering industry, has good position to contribute with the expansion and diversification of biodiesel, in regions naturally vocationated by the development of the chicken slaughter industry. Moreover, this kind of oil does not compete with the food chain. The reaction of the chicken oil with short-chains alcohols using heterogeneous catalyst allow greatly the cost-cutting, by the fact that heterogeneous catalyst can be reusable in the process of the production of the biodiesel, and also because the chicken oil is an offal of low added value; the same does not occur with the homogeneous catalyst. Given this, the aim of this work was to evaluate some catalysts in the production of esters from the crude and neutral chicken oil. The following catalysts were evaluated: Amberlyst-15, Aberlite IR-120, KSF, ZnO, CaO e methanol as alcohol reagent. The preliminary reactions occurred at 60°C e 80°C, with 5% of catalyst relative to the mass of oil, time of reaction of 5 hours and molar ratio alcohol:oil of 9:1. In this conditions, the catalyst which showed higher conversions, around 77% in esters in the preliminary tests, was the calcium oxide (CaO). A pretreatment was made with the chicken oil, with the aim of improve its properties, reducing its acidity, and with that, a performance comparative outline was made between the crude oil and the neutral one. This comparision allowed the analysis of the use effect of heterogeneuous catalysts that preaches the benefits of using impure oils in biodiesel production reactions. New tests were made with the catalyst CaO by an experimental design in which 3 variables of the transesterification reaction were evaluated: temperature, molar ratio alcohol:oil, and percentage by weight of catalyst. The highest conversions were obtained in the order of 79.8% and 83% for crude and neutral oil respectively, in the conditions of 90ºC of temperature, molar ratio alcohol:oil of 6:1 and 4% in weight of catalyst. The kinetics of the reaction was also evaluated in the following conditions: temperatures of 40ºC, 60ºC and 80ºC, methanol molar ratio: 9:1 oil and 4% by weight of catalyst; in the kinetics tests were obtained conversions of up to 94.11% ester with reaction time of 24 hours. The obtained data of the best performance of the kinetics were used for the evaluation of the mathematical modeling.Os biocombustíveis tem assumido um papel cada vez mais importante diante dos impactos ambientais e econômicos causados pelos combustíveis fósseis. O biodiesel figura como um dos mais importantes biocombustíveis no atual cenário de ampliação de combustíveis renováveis na matriz energética. A transesterificação tem prevalecido como sendo o processo mais empregado pelas indústrias produtoras desse biocombustível. Além disso, o óleo de frango, resíduo da indústria frigorífica, tem boas condições de contribuir com a ampliação e diversificação da oferta de biodiesel em regiões naturalmente vocacionadas pelo desenvolvimento da indústria de abate de frango. Ademais, esse tipo de óleo não compete com a cadeia de alimentos. A reação do óleo de frango com álcoois de cadeia curta empregando catalisadores heterogêneos possibilitam largamente a redução de custos, pelo fato de que catalisadores heterogêneos podem ser reutilizados no processo de produção de biodiesel, e também pelo fato de o óleo de frango ser um resíduo de baixo valor agregado; o mesmo não ocorre com a catálise homogênea. Diante disso, o objetivo desse trabalho foi avaliar alguns catalisadores na produção de ésteres a partir do óleo de frango bruto e neutro. Foram avaliados os seguintes catalisadores: Amberlyst-15, Aberlite IR-120, KSF, ZnO, CaO e metanol como álcool reagente. As reações preliminares ocorreram a 60°C e 80°C, com 5% de catalisador em relação a massa de óleo, tempo de reação de 5 horas e razão molar álcool:óleo de 9:1. Nessas condições, o catalisador que apresentou maiores conversões, em torno de 77% em ésteres nos ensaios preliminares, foi o óxido de cálcio (CaO). Foi realizado um pré-tratamento com o óleo de frango, visando melhorar suas propriedades, reduzindo sua acidez, e com isso, esboçou-se um comparativo de desempenho entre o óleo bruto e o óleo neutro. Tal comparativo permitiu a análise do efeito do emprego de catalisadores heterogêneos que prega o benefício do uso de óleos impuros nas reações de produção de biodiesel. Foram realizados novos testes com o catalisador CaO por meio de um planejamento experimental no qual foram avaliados 3 variáveis da reação de transesterificação: temperatura, razão molar álcool:óleo, e percentagem mássica de catalisador. As maiores conversões obtidas foram da ordem de 79,8% e 83% para os óleos bruto e neutro respectivamente, nas condições de 90ºC de temperatura, razão molar álcool:óleo de 6:1 e 4% em massa de catalisador. Avaliou-se também a cinética da reação nas seguintes condições: temperaturas de 40ºC, 60ºC e 80ºC, razão molar metanol:óleo de 9:1 e 4% em massa de catalisador; nos ensaios cinéticos foram obtidos conversões de até 94,11% de éster com tempo reacional de 24 horas. Os dados obtidos do melhor desempenho da cinética foram empregados para a avaliação da modelagem matemática.Made available in DSpace on 2017-07-10T17:59:27Z (GMT). No. of bitstreams: 1 Willian Secco.pdf: 1974581 bytes, checksum: 429ddde6626b1b1db2dede74db8d187b (MD5) Previous issue date: 2013-02-08application/pdfporUniversidade Estadual do Oeste do ParanaPrograma de Pós-Graduação Stricto Sensu em BioenergiaUNIOESTEBRBiocombustíveisTransesterificaçãoÓleo de frangoCatalisadoresHeterogêneosBioenergiaBiodieselÓleos animais como combustíveisFontes alternativas de energiaTrans oilChickenCatalystsHeterogeneousCNPQ::ENGENHARIAS::ENGENHARIA QUIMICA::TECNOLOGIA QUIMICATransesterificação do óleo de frango empregando diferentes catalisadoresTranesterification oil chicken using different catalystsinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/masterThesisinfo:eu-repo/semantics/openAccessreponame:Biblioteca Digital de Teses e Dissertações do UNIOESTEinstname:Universidade Estadual do Oeste do Paraná (UNIOESTE)instacron:UNIOESTEORIGINALWillian Secco.pdfapplication/pdf1974581http://tede.unioeste.br:8080/tede/bitstream/tede/1793/1/Willian+Secco.pdf429ddde6626b1b1db2dede74db8d187bMD51tede/17932017-07-10 14:59:27.584oai:tede.unioeste.br:tede/1793Biblioteca Digital de Teses e Dissertaçõeshttp://tede.unioeste.br/PUBhttp://tede.unioeste.br/oai/requestbiblioteca.repositorio@unioeste.bropendoar:2017-07-10T17:59:27Biblioteca Digital de Teses e Dissertações do UNIOESTE - Universidade Estadual do Oeste do Paraná (UNIOESTE)false
dc.title.por.fl_str_mv Transesterificação do óleo de frango empregando diferentes catalisadores
dc.title.alternative.eng.fl_str_mv Tranesterification oil chicken using different catalysts
title Transesterificação do óleo de frango empregando diferentes catalisadores
spellingShingle Transesterificação do óleo de frango empregando diferentes catalisadores
Secco, Willian
Transesterificação
Óleo de frango
Catalisadores
Heterogêneos
Bioenergia
Biodiesel
Óleos animais como combustíveis
Fontes alternativas de energia
Trans oil
Chicken
Catalysts
Heterogeneous
CNPQ::ENGENHARIAS::ENGENHARIA QUIMICA::TECNOLOGIA QUIMICA
title_short Transesterificação do óleo de frango empregando diferentes catalisadores
title_full Transesterificação do óleo de frango empregando diferentes catalisadores
title_fullStr Transesterificação do óleo de frango empregando diferentes catalisadores
title_full_unstemmed Transesterificação do óleo de frango empregando diferentes catalisadores
title_sort Transesterificação do óleo de frango empregando diferentes catalisadores
author Secco, Willian
author_facet Secco, Willian
author_role author
dc.contributor.advisor1.fl_str_mv Silva, Edson Antônio Alves da
dc.contributor.advisor1ID.fl_str_mv CPF:64656675920
dc.contributor.advisor1Lattes.fl_str_mv http://lattes.cnpq.br/9304493875700070
dc.contributor.referee1.fl_str_mv Bariccatti, Reinaldo Aparecido
dc.contributor.referee1ID.fl_str_mv CPF:08813157886
dc.contributor.referee1Lattes.fl_str_mv http://lattes.cnpq.br/8065417966435303
dc.contributor.referee2.fl_str_mv Silva, Camila da
dc.contributor.referee2ID.fl_str_mv CPF:03335209982
dc.contributor.referee2Lattes.fl_str_mv http://lattes.cnpq.br/0151285357488920
dc.contributor.authorID.fl_str_mv CPF:00821580965
dc.contributor.authorLattes.fl_str_mv http://lattes.cnpq.br/1737708269881791
dc.contributor.author.fl_str_mv Secco, Willian
contributor_str_mv Silva, Edson Antônio Alves da
Bariccatti, Reinaldo Aparecido
Silva, Camila da
dc.subject.por.fl_str_mv Transesterificação
Óleo de frango
Catalisadores
Heterogêneos
Bioenergia
Biodiesel
Óleos animais como combustíveis
Fontes alternativas de energia
topic Transesterificação
Óleo de frango
Catalisadores
Heterogêneos
Bioenergia
Biodiesel
Óleos animais como combustíveis
Fontes alternativas de energia
Trans oil
Chicken
Catalysts
Heterogeneous
CNPQ::ENGENHARIAS::ENGENHARIA QUIMICA::TECNOLOGIA QUIMICA
dc.subject.eng.fl_str_mv Trans oil
Chicken
Catalysts
Heterogeneous
dc.subject.cnpq.fl_str_mv CNPQ::ENGENHARIAS::ENGENHARIA QUIMICA::TECNOLOGIA QUIMICA
description The biofuel has been assuming an incresingly important role on the environmental and economic impacts caused by fossil fuels. The biodiesel represents one of the most important biofuel in the current scenery of the expanding renewable fuels, in the energy matrix. The transesterification has prevailed as the companies, which produce this biofuel, most used process. Furthermore, the chicken oil, offal of the slaughtering industry, has good position to contribute with the expansion and diversification of biodiesel, in regions naturally vocationated by the development of the chicken slaughter industry. Moreover, this kind of oil does not compete with the food chain. The reaction of the chicken oil with short-chains alcohols using heterogeneous catalyst allow greatly the cost-cutting, by the fact that heterogeneous catalyst can be reusable in the process of the production of the biodiesel, and also because the chicken oil is an offal of low added value; the same does not occur with the homogeneous catalyst. Given this, the aim of this work was to evaluate some catalysts in the production of esters from the crude and neutral chicken oil. The following catalysts were evaluated: Amberlyst-15, Aberlite IR-120, KSF, ZnO, CaO e methanol as alcohol reagent. The preliminary reactions occurred at 60°C e 80°C, with 5% of catalyst relative to the mass of oil, time of reaction of 5 hours and molar ratio alcohol:oil of 9:1. In this conditions, the catalyst which showed higher conversions, around 77% in esters in the preliminary tests, was the calcium oxide (CaO). A pretreatment was made with the chicken oil, with the aim of improve its properties, reducing its acidity, and with that, a performance comparative outline was made between the crude oil and the neutral one. This comparision allowed the analysis of the use effect of heterogeneuous catalysts that preaches the benefits of using impure oils in biodiesel production reactions. New tests were made with the catalyst CaO by an experimental design in which 3 variables of the transesterification reaction were evaluated: temperature, molar ratio alcohol:oil, and percentage by weight of catalyst. The highest conversions were obtained in the order of 79.8% and 83% for crude and neutral oil respectively, in the conditions of 90ºC of temperature, molar ratio alcohol:oil of 6:1 and 4% in weight of catalyst. The kinetics of the reaction was also evaluated in the following conditions: temperatures of 40ºC, 60ºC and 80ºC, methanol molar ratio: 9:1 oil and 4% by weight of catalyst; in the kinetics tests were obtained conversions of up to 94.11% ester with reaction time of 24 hours. The obtained data of the best performance of the kinetics were used for the evaluation of the mathematical modeling.
publishDate 2013
dc.date.available.fl_str_mv 2013-12-20
dc.date.issued.fl_str_mv 2013-02-08
dc.date.accessioned.fl_str_mv 2017-07-10T17:59:27Z
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dc.identifier.citation.fl_str_mv SECCO, Willian. Tranesterification oil chicken using different catalysts. 2013. 101 f. Dissertação (Mestrado em Biocombustíveis) - Universidade Estadual do Oeste do Parana, Toledo, 2013.
dc.identifier.uri.fl_str_mv http://tede.unioeste.br:8080/tede/handle/tede/1793
identifier_str_mv SECCO, Willian. Tranesterification oil chicken using different catalysts. 2013. 101 f. Dissertação (Mestrado em Biocombustíveis) - Universidade Estadual do Oeste do Parana, Toledo, 2013.
url http://tede.unioeste.br:8080/tede/handle/tede/1793
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dc.publisher.department.fl_str_mv Biocombustíveis
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