Obtenção de biodiesel a partir de óleos e gorduras residuais
Autor(a) principal: | |
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Data de Publicação: | 2019 |
Tipo de documento: | Tese |
Idioma: | por |
Título da fonte: | Biblioteca Digital de Teses e Dissertações do UNIOESTE |
Texto Completo: | http://tede.unioeste.br/handle/tede/4176 |
Resumo: | The transesterification from the grease trap waste (GTW) using pressurized ethanol in a catalyst free medium, aiming the continuous production of fatty acid ethyl esters (FAEE) was studied. The lipid fraction of the grease trap waste was separated and characterized, as well as it was used to conduct the reactions by evaluating the operational variables in order to maximize the formation of GTW, the two-step reaction, the addition of different water contents in ethanol, and the thermal decomposition of fatty acids. The RCG lipids showed a high content of free fatty acids, and the main fatty acids identified were oleic and linoleic. The results obtained demonstrate that the higher availability of ethanol and the increase in pressure and temperature resulted in higher yields. For the reaction performed in one step the maximum yield of FAEE was ~93% and the two step reaction increased the yield to ~96% at 300 °C, 20 MPa, oil/ethanol ratio of 1:2 and 40 minutes. When using the addition of water in ethanol in the reaction medium up to 2.5 wt% of water led to the increase of the esters in low residence time, and with the increase of the reaction time the yield was not affected compared to the reaction without addition of water, effect similar to that observed with 5 wt% water. With the use of 7.5 and 10 wt% water, the yield of esters was reduced. At the temperature > 300 °C and longer residence times the thermal degradation of the fatty acid esters, mainly of ethyl linoleate and with that the reduction of the yield of FAEE, occurred. The highest ester yield in the reactions with addition of water was 92.6%, at 300 °C, 30 min of reaction and 2.5 wt% of water in ethanol, in which condition the presence of ~5.5% of unreacted compounds (monoglycerides, diglycerides and triglycerides). The obtained results showed that the addition of water in ethanol shows similar yield to the reaction conducted without addition of water, which can reduce ethanol-related production costs. The lipid fraction of RCG can be transformed into biodiesel using ethanol from the two-step reaction. |
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Sampaio, Silvio Césarhttp://lattes.cnpq.br/9197019775809808Silva, Camila dahttp://lattes.cnpq.br/0151285357488920Reis, Ralpho Rinaldo doshttp://lattes.cnpq.br/0979626502949916Silva, Camila dahttp://lattes.cnpq.br/0151285357488920Santos, Katia Andressahttp://lattes.cnpq.br/5407907806194473Vilas Boas, Marcio Antoniohttp://lattes.cnpq.br/8467243260512730Costa, Monica Sarolli Silva de Mendonçahttp://lattes.cnpq.br/2379457318731477http://lattes.cnpq.br/3599899956230209Trentini, Caroline Portilho2019-04-03T13:58:24Z2019-01-25TRENTINI, Caroline Portilho. Obtenção de biodiesel a partir de óleos e gorduras residuais. 2019. 72 f. Tese (Programa de Pós-Graduação em Engenharia Agrícola) - Universidade Estadual do Oeste do Paraná, Cascavel, 2019.http://tede.unioeste.br/handle/tede/4176The transesterification from the grease trap waste (GTW) using pressurized ethanol in a catalyst free medium, aiming the continuous production of fatty acid ethyl esters (FAEE) was studied. The lipid fraction of the grease trap waste was separated and characterized, as well as it was used to conduct the reactions by evaluating the operational variables in order to maximize the formation of GTW, the two-step reaction, the addition of different water contents in ethanol, and the thermal decomposition of fatty acids. The RCG lipids showed a high content of free fatty acids, and the main fatty acids identified were oleic and linoleic. The results obtained demonstrate that the higher availability of ethanol and the increase in pressure and temperature resulted in higher yields. For the reaction performed in one step the maximum yield of FAEE was ~93% and the two step reaction increased the yield to ~96% at 300 °C, 20 MPa, oil/ethanol ratio of 1:2 and 40 minutes. When using the addition of water in ethanol in the reaction medium up to 2.5 wt% of water led to the increase of the esters in low residence time, and with the increase of the reaction time the yield was not affected compared to the reaction without addition of water, effect similar to that observed with 5 wt% water. With the use of 7.5 and 10 wt% water, the yield of esters was reduced. At the temperature > 300 °C and longer residence times the thermal degradation of the fatty acid esters, mainly of ethyl linoleate and with that the reduction of the yield of FAEE, occurred. The highest ester yield in the reactions with addition of water was 92.6%, at 300 °C, 30 min of reaction and 2.5 wt% of water in ethanol, in which condition the presence of ~5.5% of unreacted compounds (monoglycerides, diglycerides and triglycerides). The obtained results showed that the addition of water in ethanol shows similar yield to the reaction conducted without addition of water, which can reduce ethanol-related production costs. The lipid fraction of RCG can be transformed into biodiesel using ethanol from the two-step reaction.A transesterificação a partir do resíduo de caixa de gordura (RCG) utilizando etanol pressurizado em meio livre de catalisador, visando a produção contínua de ésteres etílicos de ácidos graxos (EEAG) foi estudada. A fração lipídica do RCG foi separada, caracterizada e utilizada para a condução das reações avaliando-se as variáveis operacionais, buscando maximizar a formação de EEAG, a reação de duas etapas, a adição de diferentes teores de água em etanol e a decomposição térmica dos ácidos graxos. Os lipídeos de RCG demonstraram um alto teor de ácidos graxos livres, sendo que os principais ácidos graxos identificados em sua composição foram o oleico e o linoleico. Os resultados obtidos demonstram que a maior disponibilidade de etanol e o aumento da pressão e da temperatura proporcionaram a obtenção de maiores rendimentos. Para a reação realizada em uma etapa o rendimento máximo de EEAG foi de ~93% e a reação em duas etapas aumentou o rendimento para ~96% a 300 °C, 20 MPa, razão óleo/etanol de 1:2 e 40 minutos. Quando utilizada a adição de água em etanol no meio reacional até 2,5% houve aumento dos ésteres em baixos tempo de residência, sendo que com o aumento do tempo reacional o rendimento não foi afetado comparado à reação sem adição de água, efeito semelhante ao observado com 5% de água. Com a utilização de 7,5 e 10% de água ocorreu a redução do rendimento em ésteres. A temperatura > 300 °C e maiores tempos de residência promoveram a degradação térmica dos ésteres de ácidos graxos, principalmente do linoleato de etila, e com isso a redução do rendimento de EEAG. O maior rendimento em éster nas reações com adição de água foi de 92,6% a 300 °C, 30 min de reação e 2,5% de água em etanol, sendo que nesta condição foi verificada a presença de ~5,5% de compostos não reagidos (monoglicerídeos, diglicerídeos e triglicerídeos). Os resultados obtidos demonstraram que a adição de água em etanol apresenta rendimento similar à reação conduzida sem adição de água, sendo que com isso pode-se reduzir os custos de produção relacionados ao etanol, podendo-se, assim, a fração lipídica de RCG ser transformada em biodiesel utilizando o etanol a partir da reação de duas etapas.Submitted by Neusa Fagundes (neusa.fagundes@unioeste.br) on 2019-04-03T13:58:24Z No. of bitstreams: 2 Caroline P_Trentini2019.pdf: 1095217 bytes, checksum: 8326a603d45a0f0c0c7df740e144e55e (MD5) license_rdf: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5)Made available in DSpace on 2019-04-03T13:58:24Z (GMT). No. of bitstreams: 2 Caroline P_Trentini2019.pdf: 1095217 bytes, checksum: 8326a603d45a0f0c0c7df740e144e55e (MD5) license_rdf: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5) Previous issue date: 2019-01-25Coordenação de Aperfeiçoamento de Pessoal de Nível Superior - CAPESapplication/pdfpor6588633818200016417500Universidade Estadual do Oeste do ParanáCascavelPrograma de Pós-Graduação em Engenharia AgrícolaUNIOESTEBrasilCentro de Ciências Exatas e Tecnológicashttp://creativecommons.org/licenses/by-nc-nd/4.0/info:eu-repo/semantics/openAccessResíduo de caixa de gorduraProcesso contínuoÉsteres etílicosÁguaGrease trap wasteContinuous processEthyl estersWaterCIENCIAS AGRARIAS::ENGENHARIA AGRICOLAObtenção de biodiesel a partir de óleos e gorduras residuaisBiodiesel obtention from waste oils and greaseinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/doctoralThesis-5347692450416052129600600600600221437444286838201591854457215887615552075167498588264571reponame:Biblioteca Digital de Teses e Dissertações do UNIOESTEinstname:Universidade Estadual do Oeste do Paraná (UNIOESTE)instacron:UNIOESTEORIGINALCaroline P_Trentini2019.pdfCaroline P_Trentini2019.pdfapplication/pdf1095217http://tede.unioeste.br:8080/tede/bitstream/tede/4176/5/Caroline+P_Trentini2019.pdf8326a603d45a0f0c0c7df740e144e55eMD55CC-LICENSElicense_urllicense_urltext/plain; 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dc.title.por.fl_str_mv |
Obtenção de biodiesel a partir de óleos e gorduras residuais |
dc.title.alternative.eng.fl_str_mv |
Biodiesel obtention from waste oils and grease |
title |
Obtenção de biodiesel a partir de óleos e gorduras residuais |
spellingShingle |
Obtenção de biodiesel a partir de óleos e gorduras residuais Trentini, Caroline Portilho Resíduo de caixa de gordura Processo contínuo Ésteres etílicos Água Grease trap waste Continuous process Ethyl esters Water CIENCIAS AGRARIAS::ENGENHARIA AGRICOLA |
title_short |
Obtenção de biodiesel a partir de óleos e gorduras residuais |
title_full |
Obtenção de biodiesel a partir de óleos e gorduras residuais |
title_fullStr |
Obtenção de biodiesel a partir de óleos e gorduras residuais |
title_full_unstemmed |
Obtenção de biodiesel a partir de óleos e gorduras residuais |
title_sort |
Obtenção de biodiesel a partir de óleos e gorduras residuais |
author |
Trentini, Caroline Portilho |
author_facet |
Trentini, Caroline Portilho |
author_role |
author |
dc.contributor.advisor1.fl_str_mv |
Sampaio, Silvio César |
dc.contributor.advisor1Lattes.fl_str_mv |
http://lattes.cnpq.br/9197019775809808 |
dc.contributor.advisor-co1.fl_str_mv |
Silva, Camila da |
dc.contributor.advisor-co1Lattes.fl_str_mv |
http://lattes.cnpq.br/0151285357488920 |
dc.contributor.advisor-co2.fl_str_mv |
Reis, Ralpho Rinaldo dos |
dc.contributor.advisor-co2Lattes.fl_str_mv |
http://lattes.cnpq.br/0979626502949916 |
dc.contributor.referee1.fl_str_mv |
Silva, Camila da |
dc.contributor.referee1Lattes.fl_str_mv |
http://lattes.cnpq.br/0151285357488920 |
dc.contributor.referee2.fl_str_mv |
Santos, Katia Andressa |
dc.contributor.referee2Lattes.fl_str_mv |
http://lattes.cnpq.br/5407907806194473 |
dc.contributor.referee3.fl_str_mv |
Vilas Boas, Marcio Antonio |
dc.contributor.referee3Lattes.fl_str_mv |
http://lattes.cnpq.br/8467243260512730 |
dc.contributor.referee4.fl_str_mv |
Costa, Monica Sarolli Silva de Mendonça |
dc.contributor.referee4Lattes.fl_str_mv |
http://lattes.cnpq.br/2379457318731477 |
dc.contributor.authorLattes.fl_str_mv |
http://lattes.cnpq.br/3599899956230209 |
dc.contributor.author.fl_str_mv |
Trentini, Caroline Portilho |
contributor_str_mv |
Sampaio, Silvio César Silva, Camila da Reis, Ralpho Rinaldo dos Silva, Camila da Santos, Katia Andressa Vilas Boas, Marcio Antonio Costa, Monica Sarolli Silva de Mendonça |
dc.subject.por.fl_str_mv |
Resíduo de caixa de gordura Processo contínuo Ésteres etílicos Água |
topic |
Resíduo de caixa de gordura Processo contínuo Ésteres etílicos Água Grease trap waste Continuous process Ethyl esters Water CIENCIAS AGRARIAS::ENGENHARIA AGRICOLA |
dc.subject.eng.fl_str_mv |
Grease trap waste Continuous process Ethyl esters Water |
dc.subject.cnpq.fl_str_mv |
CIENCIAS AGRARIAS::ENGENHARIA AGRICOLA |
description |
The transesterification from the grease trap waste (GTW) using pressurized ethanol in a catalyst free medium, aiming the continuous production of fatty acid ethyl esters (FAEE) was studied. The lipid fraction of the grease trap waste was separated and characterized, as well as it was used to conduct the reactions by evaluating the operational variables in order to maximize the formation of GTW, the two-step reaction, the addition of different water contents in ethanol, and the thermal decomposition of fatty acids. The RCG lipids showed a high content of free fatty acids, and the main fatty acids identified were oleic and linoleic. The results obtained demonstrate that the higher availability of ethanol and the increase in pressure and temperature resulted in higher yields. For the reaction performed in one step the maximum yield of FAEE was ~93% and the two step reaction increased the yield to ~96% at 300 °C, 20 MPa, oil/ethanol ratio of 1:2 and 40 minutes. When using the addition of water in ethanol in the reaction medium up to 2.5 wt% of water led to the increase of the esters in low residence time, and with the increase of the reaction time the yield was not affected compared to the reaction without addition of water, effect similar to that observed with 5 wt% water. With the use of 7.5 and 10 wt% water, the yield of esters was reduced. At the temperature > 300 °C and longer residence times the thermal degradation of the fatty acid esters, mainly of ethyl linoleate and with that the reduction of the yield of FAEE, occurred. The highest ester yield in the reactions with addition of water was 92.6%, at 300 °C, 30 min of reaction and 2.5 wt% of water in ethanol, in which condition the presence of ~5.5% of unreacted compounds (monoglycerides, diglycerides and triglycerides). The obtained results showed that the addition of water in ethanol shows similar yield to the reaction conducted without addition of water, which can reduce ethanol-related production costs. The lipid fraction of RCG can be transformed into biodiesel using ethanol from the two-step reaction. |
publishDate |
2019 |
dc.date.accessioned.fl_str_mv |
2019-04-03T13:58:24Z |
dc.date.issued.fl_str_mv |
2019-01-25 |
dc.type.status.fl_str_mv |
info:eu-repo/semantics/publishedVersion |
dc.type.driver.fl_str_mv |
info:eu-repo/semantics/doctoralThesis |
format |
doctoralThesis |
status_str |
publishedVersion |
dc.identifier.citation.fl_str_mv |
TRENTINI, Caroline Portilho. Obtenção de biodiesel a partir de óleos e gorduras residuais. 2019. 72 f. Tese (Programa de Pós-Graduação em Engenharia Agrícola) - Universidade Estadual do Oeste do Paraná, Cascavel, 2019. |
dc.identifier.uri.fl_str_mv |
http://tede.unioeste.br/handle/tede/4176 |
identifier_str_mv |
TRENTINI, Caroline Portilho. Obtenção de biodiesel a partir de óleos e gorduras residuais. 2019. 72 f. Tese (Programa de Pós-Graduação em Engenharia Agrícola) - Universidade Estadual do Oeste do Paraná, Cascavel, 2019. |
url |
http://tede.unioeste.br/handle/tede/4176 |
dc.language.iso.fl_str_mv |
por |
language |
por |
dc.relation.program.fl_str_mv |
-5347692450416052129 |
dc.relation.confidence.fl_str_mv |
600 600 600 600 |
dc.relation.department.fl_str_mv |
2214374442868382015 |
dc.relation.cnpq.fl_str_mv |
9185445721588761555 |
dc.relation.sponsorship.fl_str_mv |
2075167498588264571 |
dc.rights.driver.fl_str_mv |
http://creativecommons.org/licenses/by-nc-nd/4.0/ info:eu-repo/semantics/openAccess |
rights_invalid_str_mv |
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 Estadual do Oeste do Paraná Cascavel |
dc.publisher.program.fl_str_mv |
Programa de Pós-Graduação em Engenharia Agrícola |
dc.publisher.initials.fl_str_mv |
UNIOESTE |
dc.publisher.country.fl_str_mv |
Brasil |
dc.publisher.department.fl_str_mv |
Centro de Ciências Exatas e Tecnológicas |
publisher.none.fl_str_mv |
Universidade Estadual do Oeste do Paraná Cascavel |
dc.source.none.fl_str_mv |
reponame:Biblioteca Digital de Teses e Dissertações do UNIOESTE instname:Universidade Estadual do Oeste do Paraná (UNIOESTE) instacron:UNIOESTE |
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Universidade Estadual do Oeste do Paraná (UNIOESTE) |
instacron_str |
UNIOESTE |
institution |
UNIOESTE |
reponame_str |
Biblioteca Digital de Teses e Dissertações do UNIOESTE |
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Biblioteca Digital de Teses e Dissertações do UNIOESTE |
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