CENTRAL COMPOSITE DESIGN APPLIED TO BIOQUEROSENE OBTAINING SYSTEM VIA HETEROGENEOUS CATALYSIS

Detalhes bibliográficos
Autor(a) principal: da Ponte, Flávio Albuquerque Ferreira
Data de Publicação: 2017
Outros Autores: Rodrigues, Jailson Silva, Malveira, Jackson de Queiroz, Maciel, Islanya Aguiar, Albuquerque, Mônica Castelo Guimarães
Tipo de documento: Artigo
Idioma: por
Título da fonte: The Journal of Engineering and Exact Sciences
Texto Completo: https://periodicos.ufv.br/jcec/article/view/2446941603032017418
Resumo: In this work biokerosene was produced by the esterification reaction (using heterogeneous catalyst such as AmberlystTM 15) of free fatty acids of C6 to C16 carbon atoms derived from babassu oil (Orbinya speciosa) using a 23 factorial experimental design with central composite. Scanning electron microscopy morphology and the thermogravimetry analysis was used to indicate the working range of the catalyst. The process parameters studied were the reaction temperature between 70 °C to 100 °C, catalyst concentration between 5 % to 10 % and reaction time between 240 minute to 480 minute. As the factorial design response parameter was evaluated the methyl esters content. The process optimization was performed using the response surface methodology (RSM) and the polynomial model of second order. It was observed that the most influential process variables were the reaction temperature and time, the highest conversion of methyl esters was obtained with 7.5 % catalyst; reaction temperature of 85 °C and 360 minutes of reaction. The best conversion of the reaction was 94.7 % on biofuel. Utilizing the MRS with second-order polynomial model, the optimized conditions achieved for the esterification reaction with Amberlyst® 15 were: a temperature of 90.0 ° C, catalyst amount of 7.3 %, and reaction time 338.2 minutes . The expected theoretical yield of conversion into free fatty acids from C6 to C16 carbon atoms in biokerosene was 95.7 %.
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spelling CENTRAL COMPOSITE DESIGN APPLIED TO BIOQUEROSENE OBTAINING SYSTEM VIA HETEROGENEOUS CATALYSISPLANEJAMENTO COMPOSTO CENTRAL APLICADO A SISTEMA DE OBTENÇÃO DE BIOQUEROSENE VIA CATÁLISE HETEROGÊNEACentral composite designBiokeroseneFree fatty acidsBabassu oilHeterogeneous catalystResponse surface methodololy.Planejamento composto central (PCC)BioqueroseneÁcidos graxos livresÓleo de babaçuCatalisador heterogêneoMetodologia de superfície de respostaIn this work biokerosene was produced by the esterification reaction (using heterogeneous catalyst such as AmberlystTM 15) of free fatty acids of C6 to C16 carbon atoms derived from babassu oil (Orbinya speciosa) using a 23 factorial experimental design with central composite. Scanning electron microscopy morphology and the thermogravimetry analysis was used to indicate the working range of the catalyst. The process parameters studied were the reaction temperature between 70 °C to 100 °C, catalyst concentration between 5 % to 10 % and reaction time between 240 minute to 480 minute. As the factorial design response parameter was evaluated the methyl esters content. The process optimization was performed using the response surface methodology (RSM) and the polynomial model of second order. It was observed that the most influential process variables were the reaction temperature and time, the highest conversion of methyl esters was obtained with 7.5 % catalyst; reaction temperature of 85 °C and 360 minutes of reaction. The best conversion of the reaction was 94.7 % on biofuel. Utilizing the MRS with second-order polynomial model, the optimized conditions achieved for the esterification reaction with Amberlyst® 15 were: a temperature of 90.0 ° C, catalyst amount of 7.3 %, and reaction time 338.2 minutes . The expected theoretical yield of conversion into free fatty acids from C6 to C16 carbon atoms in biokerosene was 95.7 %.Neste trabalho foi produzido bioquerosene pela reação de esterificação (utilizando o Amberlyst® 15 como catalisador heterogêneo) dos ácidos graxos livres de C6 a C16 átomos de carbono provenientes do óleo de babaçu (Orbignya speciosa) utilizando um planejamento de experimento fatorial 23 com composto central. A análise termogravimétria foi utilizada para indicar a faixa de trabalho do catalisador e a microscopia eletrônica de varredura, a morfologia. Os parâmetros de processo estudados foram a temperatura de reação entre 70 °C e 100 °C, a concentração em massa de catalisador entre 5 % e 10 % e o tempo de reação entre 240 minutos e 480 minutos. Como parâmetro de resposta do planejamento experimental foi avaliado o teor em massa de metil ésteres. A otimização do processo foi realizada através da metodologia de superfície de resposta (MSR) e o modelo polinomial de segunda ordem. Foi observado que a variável de processo de maior influência foi a temperatura de reação, sendo que a maior conversão de ésteres foi obtida com 7,5 % de catalisador; temperatura de reação de 85 °C e com um tempo de 360 minutos de reação. Com esses parâmetros a conversão alcançada foi de 94,7 % em biocombustível. Utilizando a MRS, com modelo polinomial de segunda ordem, as condições otimizadas obtidas para a reação de esterificação com Amberlyst® 15 foram: temperatura de 90,0 °C, quantidade de catalisador de 7,3 % e tempo reacional de 338,2 minutos. O rendimento teórico da conversão previsto para os ácidos graxos livres de C6 a C16 átomos de carbono em bioquerosene foi de 95,7 %. Esta pesquisa foi apoiada pela Universidade Federal do Ceará (UFC), Laboratório de Imagem Central Analítica da UFC, Fundação Núcleo de Tecnologia Industrial do Ceará (NUTEC) e financiada pelo Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq) e pela Fundação Cearense de Apoio ao Desenvolvimento Científico e Tecnológico (FUNCAP).Universidade Federal de Viçosa - UFV2017-03-08info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionapplication/kswpshttps://periodicos.ufv.br/jcec/article/view/244694160303201741810.18540/jcecvl3iss3pp418-435The Journal of Engineering and Exact Sciences; Vol. 3 No. 3 (2017); 418-435The Journal of Engineering and Exact Sciences; Vol. 3 Núm. 3 (2017); 418-435The Journal of Engineering and Exact Sciences; v. 3 n. 3 (2017); 418-4352527-1075reponame:The Journal of Engineering and Exact Sciencesinstname:Universidade Federal de Viçosa (UFV)instacron:UFVporhttps://periodicos.ufv.br/jcec/article/view/2446941603032017418/pdfda Ponte, Flávio Albuquerque FerreiraRodrigues, Jailson SilvaMalveira, Jackson de QueirozMaciel, Islanya AguiarAlbuquerque, Mônica Castelo Guimarãesinfo:eu-repo/semantics/openAccess2020-07-14T22:33:54Zoai:ojs.periodicos.ufv.br:article/2179Revistahttp://www.seer.ufv.br/seer/rbeq2/index.php/req2/oai2527-10752527-1075opendoar:2020-07-14T22:33:54The Journal of Engineering and Exact Sciences - Universidade Federal de Viçosa (UFV)false
dc.title.none.fl_str_mv CENTRAL COMPOSITE DESIGN APPLIED TO BIOQUEROSENE OBTAINING SYSTEM VIA HETEROGENEOUS CATALYSIS
PLANEJAMENTO COMPOSTO CENTRAL APLICADO A SISTEMA DE OBTENÇÃO DE BIOQUEROSENE VIA CATÁLISE HETEROGÊNEA
title CENTRAL COMPOSITE DESIGN APPLIED TO BIOQUEROSENE OBTAINING SYSTEM VIA HETEROGENEOUS CATALYSIS
spellingShingle CENTRAL COMPOSITE DESIGN APPLIED TO BIOQUEROSENE OBTAINING SYSTEM VIA HETEROGENEOUS CATALYSIS
da Ponte, Flávio Albuquerque Ferreira
Central composite design
Biokerosene
Free fatty acids
Babassu oil
Heterogeneous catalyst
Response surface methodololy.
Planejamento composto central (PCC)
Bioquerosene
Ácidos graxos livres
Óleo de babaçu
Catalisador heterogêneo
Metodologia de superfície de resposta
title_short CENTRAL COMPOSITE DESIGN APPLIED TO BIOQUEROSENE OBTAINING SYSTEM VIA HETEROGENEOUS CATALYSIS
title_full CENTRAL COMPOSITE DESIGN APPLIED TO BIOQUEROSENE OBTAINING SYSTEM VIA HETEROGENEOUS CATALYSIS
title_fullStr CENTRAL COMPOSITE DESIGN APPLIED TO BIOQUEROSENE OBTAINING SYSTEM VIA HETEROGENEOUS CATALYSIS
title_full_unstemmed CENTRAL COMPOSITE DESIGN APPLIED TO BIOQUEROSENE OBTAINING SYSTEM VIA HETEROGENEOUS CATALYSIS
title_sort CENTRAL COMPOSITE DESIGN APPLIED TO BIOQUEROSENE OBTAINING SYSTEM VIA HETEROGENEOUS CATALYSIS
author da Ponte, Flávio Albuquerque Ferreira
author_facet da Ponte, Flávio Albuquerque Ferreira
Rodrigues, Jailson Silva
Malveira, Jackson de Queiroz
Maciel, Islanya Aguiar
Albuquerque, Mônica Castelo Guimarães
author_role author
author2 Rodrigues, Jailson Silva
Malveira, Jackson de Queiroz
Maciel, Islanya Aguiar
Albuquerque, Mônica Castelo Guimarães
author2_role author
author
author
author
dc.contributor.author.fl_str_mv da Ponte, Flávio Albuquerque Ferreira
Rodrigues, Jailson Silva
Malveira, Jackson de Queiroz
Maciel, Islanya Aguiar
Albuquerque, Mônica Castelo Guimarães
dc.subject.por.fl_str_mv Central composite design
Biokerosene
Free fatty acids
Babassu oil
Heterogeneous catalyst
Response surface methodololy.
Planejamento composto central (PCC)
Bioquerosene
Ácidos graxos livres
Óleo de babaçu
Catalisador heterogêneo
Metodologia de superfície de resposta
topic Central composite design
Biokerosene
Free fatty acids
Babassu oil
Heterogeneous catalyst
Response surface methodololy.
Planejamento composto central (PCC)
Bioquerosene
Ácidos graxos livres
Óleo de babaçu
Catalisador heterogêneo
Metodologia de superfície de resposta
description In this work biokerosene was produced by the esterification reaction (using heterogeneous catalyst such as AmberlystTM 15) of free fatty acids of C6 to C16 carbon atoms derived from babassu oil (Orbinya speciosa) using a 23 factorial experimental design with central composite. Scanning electron microscopy morphology and the thermogravimetry analysis was used to indicate the working range of the catalyst. The process parameters studied were the reaction temperature between 70 °C to 100 °C, catalyst concentration between 5 % to 10 % and reaction time between 240 minute to 480 minute. As the factorial design response parameter was evaluated the methyl esters content. The process optimization was performed using the response surface methodology (RSM) and the polynomial model of second order. It was observed that the most influential process variables were the reaction temperature and time, the highest conversion of methyl esters was obtained with 7.5 % catalyst; reaction temperature of 85 °C and 360 minutes of reaction. The best conversion of the reaction was 94.7 % on biofuel. Utilizing the MRS with second-order polynomial model, the optimized conditions achieved for the esterification reaction with Amberlyst® 15 were: a temperature of 90.0 ° C, catalyst amount of 7.3 %, and reaction time 338.2 minutes . The expected theoretical yield of conversion into free fatty acids from C6 to C16 carbon atoms in biokerosene was 95.7 %.
publishDate 2017
dc.date.none.fl_str_mv 2017-03-08
dc.type.driver.fl_str_mv info:eu-repo/semantics/article
info:eu-repo/semantics/publishedVersion
format article
status_str publishedVersion
dc.identifier.uri.fl_str_mv https://periodicos.ufv.br/jcec/article/view/2446941603032017418
10.18540/jcecvl3iss3pp418-435
url https://periodicos.ufv.br/jcec/article/view/2446941603032017418
identifier_str_mv 10.18540/jcecvl3iss3pp418-435
dc.language.iso.fl_str_mv por
language por
dc.relation.none.fl_str_mv https://periodicos.ufv.br/jcec/article/view/2446941603032017418/pdf
dc.rights.driver.fl_str_mv info:eu-repo/semantics/openAccess
eu_rights_str_mv openAccess
dc.format.none.fl_str_mv application/kswps
dc.publisher.none.fl_str_mv Universidade Federal de Viçosa - UFV
publisher.none.fl_str_mv Universidade Federal de Viçosa - UFV
dc.source.none.fl_str_mv The Journal of Engineering and Exact Sciences; Vol. 3 No. 3 (2017); 418-435
The Journal of Engineering and Exact Sciences; Vol. 3 Núm. 3 (2017); 418-435
The Journal of Engineering and Exact Sciences; v. 3 n. 3 (2017); 418-435
2527-1075
reponame:The Journal of Engineering and Exact Sciences
instname:Universidade Federal de Viçosa (UFV)
instacron:UFV
instname_str Universidade Federal de Viçosa (UFV)
instacron_str UFV
institution UFV
reponame_str The Journal of Engineering and Exact Sciences
collection The Journal of Engineering and Exact Sciences
repository.name.fl_str_mv The Journal of Engineering and Exact Sciences - Universidade Federal de Viçosa (UFV)
repository.mail.fl_str_mv
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