Purificação da glicerina bruta obtida a partir da transesterificação do óleo de algodão

Detalhes bibliográficos
Ano de defesa: 2009
Autor(a) principal: Ferreira, Marcionila de Oliveira
Orientador(a): Pereira, Camila Gambini
Banca de defesa: Não Informado pela instituição
Tipo de documento: Dissertação
Tipo de acesso: Acesso aberto
Idioma: por
Instituição de defesa: Universidade Federal do Rio Grande do Norte
Programa de Pós-Graduação: Programa de Pós-Graduação em Engenharia Química
Departamento: Pesquisa e Desenvolvimento de Tecnologias Regionais
País: BR
Palavras-chave em Português:
Palavras-chave em Inglês:
Área do conhecimento CNPq:
Link de acesso: https://repositorio.ufrn.br/jspui/handle/123456789/15767
Resumo: The crude glycerine is a raw material that can be used in a wide variety of products. Even with all the impurities inherent in the process of being obtained, the crude glycerin is already in a marketable product. However, the market is much more favorable to the commercialization of purified glycerine. The glycerin is a byproduct gotten from the process of transesterification of waste oils and fats in the production of biodiesel. More recently, the deployment of the new Federal Law of Brazil, related to the implementation of energy resources, forces, from 2008, the increase of 2% biodiesel in diesel common with prospects for 5% (B5). Therefore, it is indispensable that new routes of purification as well as new markets are developed. The objective of this work was to purify, through ion exchange, the crude glycerin, obtained from the reaction of transesterification of cottonseed oil. The cottonseed oil was characterized as the fatty acid composition and physical-chemical properties. The process of ion exchange was conducted in batch. In this process were used strong cation, low anion resins and a mixed resin used to de-ionize water. The purified glycerin was characterized as the content of metals. Tests were performed with activated charcoal adsorption, and for this, it was made tests of time contact with coal as well as quantity of coal used. The time of activation, the amount of the activation solution, the contact time of the glycerol solution in resins, the amount and type of resin applied were evaluated. Considering the analysis made with activated charcoal, when the glycerin solution was treated using the resins individually it was observed that in the conditions for treatment with 10 g of resin, 5 hours of contact with each resin and 50 mL of glycerin solution, its conductivity decreased to a cationic resin, increased to the anionic resin and had a variable value with respect to resin mixed. In the treatment in series, there was a constant decrease in the conductivity of the solution of glycerin. Considering two types of treatment, in series and individually, the content of glycerol in glycerin pre-purified solution with the different resins varied from 12,46 to 29.51% (diluted solution). In analysis performed without the use of activated charcoal, the behavior of the conductivity of the solution of glycerin were similar to results for treatment with activated charcoal, both in series as individually. The solution of glycerin pre-purified had a glycerol content varying from 8.3 to 25.7% (diluted solution). In relation to pH, it had a behavior in accordance with the expected: acid for the glycerin solution treated with cationic resin, basic when the glycerin solution was treated with the anionic resin and neutral when treated with the mixed resin, independent of the kind of procedure used (with or without coal, resins individually or in series). In relation to the color of the glycerin pre-purified solution, the resin that showed the best result was the anionic (colorless), however this does not mean that the solution is more in pure glycerol. The chromatographic analysis of the solutions obtained after the passage through the resins indicated that the treatment was effective by the presence of only one component (glycerol), not considering the solvent of the analysis
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spelling Ferreira, Marcionila de Oliveirahttp://lattes.cnpq.br/0362693118434408http://lattes.cnpq.br/8055289812908100Sousa, Elisa Maria Bittencourt Dutra dehttp://buscatextual.cnpq.br/buscatextual/visualizacv.do?id=K4787769D1Oliveira, Humberto Neves Maia dehttp://lattes.cnpq.br/7302633941782540Oliveira, Jackson Araújo dehttp://lattes.cnpq.br/5058617634570704Pereira, Camila Gambini2014-12-17T15:01:18Z2009-07-132014-12-17T15:01:18Z2009-03-05FERREIRA, Marcionila de Oliveira. Purificação da glicerina bruta obtida a partir da transesterificação do óleo de algodão. 2009. 127 f. Dissertação (Mestrado em Pesquisa e Desenvolvimento de Tecnologias Regionais) - Universidade Federal do Rio Grande do Norte, Natal, 2009.https://repositorio.ufrn.br/jspui/handle/123456789/15767The crude glycerine is a raw material that can be used in a wide variety of products. Even with all the impurities inherent in the process of being obtained, the crude glycerin is already in a marketable product. However, the market is much more favorable to the commercialization of purified glycerine. The glycerin is a byproduct gotten from the process of transesterification of waste oils and fats in the production of biodiesel. More recently, the deployment of the new Federal Law of Brazil, related to the implementation of energy resources, forces, from 2008, the increase of 2% biodiesel in diesel common with prospects for 5% (B5). Therefore, it is indispensable that new routes of purification as well as new markets are developed. The objective of this work was to purify, through ion exchange, the crude glycerin, obtained from the reaction of transesterification of cottonseed oil. The cottonseed oil was characterized as the fatty acid composition and physical-chemical properties. The process of ion exchange was conducted in batch. In this process were used strong cation, low anion resins and a mixed resin used to de-ionize water. The purified glycerin was characterized as the content of metals. Tests were performed with activated charcoal adsorption, and for this, it was made tests of time contact with coal as well as quantity of coal used. The time of activation, the amount of the activation solution, the contact time of the glycerol solution in resins, the amount and type of resin applied were evaluated. Considering the analysis made with activated charcoal, when the glycerin solution was treated using the resins individually it was observed that in the conditions for treatment with 10 g of resin, 5 hours of contact with each resin and 50 mL of glycerin solution, its conductivity decreased to a cationic resin, increased to the anionic resin and had a variable value with respect to resin mixed. In the treatment in series, there was a constant decrease in the conductivity of the solution of glycerin. Considering two types of treatment, in series and individually, the content of glycerol in glycerin pre-purified solution with the different resins varied from 12,46 to 29.51% (diluted solution). In analysis performed without the use of activated charcoal, the behavior of the conductivity of the solution of glycerin were similar to results for treatment with activated charcoal, both in series as individually. The solution of glycerin pre-purified had a glycerol content varying from 8.3 to 25.7% (diluted solution). In relation to pH, it had a behavior in accordance with the expected: acid for the glycerin solution treated with cationic resin, basic when the glycerin solution was treated with the anionic resin and neutral when treated with the mixed resin, independent of the kind of procedure used (with or without coal, resins individually or in series). In relation to the color of the glycerin pre-purified solution, the resin that showed the best result was the anionic (colorless), however this does not mean that the solution is more in pure glycerol. The chromatographic analysis of the solutions obtained after the passage through the resins indicated that the treatment was effective by the presence of only one component (glycerol), not considering the solvent of the analysisA glicerina bruta é uma matéria-prima que pode ser usada em uma ampla variedade de produtos. Mesmo com todas as impurezas inerentes ao processo de sua obtenção, a glicerina bruta já se constitui em um subproduto vendável. Entretanto, o mercado é muito mais favorável à comercialização da glicerina purificada. A glicerina é um subproduto resultante do processo de transesterificação de óleos e gorduras residuais na produção do biodiesel. Mais recentemente, a implantação da nova Lei Federal do Brasil, relacionada à aplicação dos recursos energéticos, obriga, a partir de 2008, o acréscimo de 2% de biodiesel no diesel comum com perspectivas para 5% (B5). Dessa forma, é indispensável que novas rotas de purificação assim como novos mercados sejam desenvolvidos. O objetivo desse trabalho foi purificar, através da troca iônica, a glicerina bruta obtida da reação de transesterificação do óleo de algodão. O óleo de algodão foi caracterizado quanto à composição em ácidos graxos e quanto às propriedades físico-químicas. O processo da troca iônica foi conduzido em batelada. Foram utilizadas nesse processo as resinas catiônica forte, aniônica fraca e uma resina mista utilizada para deionizar água. A glicerina purificada foi caracterizada quanto ao teor de metais. Foram realizados ensaios de adsorção com carvão ativado, e para isto, foram feitos ensaios de tempo de contato com carvão ativado bem como quantidade de carvão ativado utilizada. Foram avaliados: o tempo de ativação, a quantidade de solução de ativação, o tempo de contato da solução de glicerina nas resinas, a quantidade e tipo de resina aplicada. Considerando as análises feitas com carvão ativado, quando a solução de glicerina foi tratada utilizando as resinas individualmente foi observado que, nas condições definidas para o tratamento com 10g de resina, 5 horas de contato com cada resina e 50 mL de solução de glicerina, sua condutividade diminuiu para a resina catiônica, aumentou para a resina aniônica e teve um valor variável com relação a resina mista. No tratamento em série, houve uma diminuição constante da condutividade da solução de glicerina. Considerando os dois tipos de tratamento, em série e individualmente, o teor de glicerol na solução de glicerina pré-purificada com as diferentes resinas variou de 12,46 a 29,51% (solução diluída). Nas análises realizadas sem o uso do carvão ativado, o comportamento da condutividade da solução de glicerina foi similar ao resultado para o tratamento com carvão ativado, tanto em série quanto individualmente. A solução de glicerina pré-purificada teve um teor de glicerol variando de 8,3 a 25,7% (solução diluída). Com relação ao pH, este teve um comportamento de acordo com o esperado: ácido para a solução de glicerina tratada com resina catiônica, básico quando a solução de glicerina foi tratada com a resina aniônica e neutro quando tratada com a resina mista, independente do tipo de procedimento utilizado (com ou sem carvão ativado, resinas individualmente ou em série). Com relação à cor da solução de glicerina pré-purificada, a resina que apresentou melhor resultado foi a aniônica (incolor), no entanto isto não quer dizer que a solução estivesse mais pura em glicerol. A análise cromatográfica das soluções obtidas após a passagem pelas resinas indicou que o tratamento foi eficaz pela presença de somente um componente (glicerol), não considerando o solvente da análiseCoordenação de Aperfeiçoamento de Pessoal de Nível Superiorapplication/pdfporUniversidade Federal do Rio Grande do NortePrograma de Pós-Graduação em Engenharia QuímicaUFRNBRPesquisa e Desenvolvimento de Tecnologias RegionaisPurificação da glicerinatroca iônicaadsorçãoGlycerin purificationion exchangeadsorptionCNPQ::ENGENHARIAS::ENGENHARIA QUIMICAPurificação da glicerina bruta obtida a partir da transesterificação do óleo de algodãoPurificação da glicerina bruta obtida a partir da transesterificação do óleo de algodãoinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/masterThesisinfo:eu-repo/semantics/openAccessreponame:Repositório Institucional da UFRNinstname:Universidade Federal do Rio Grande do Norte (UFRN)instacron:UFRNORIGINALMarcionilaOF.pdfapplication/pdf1821227https://repositorio.ufrn.br/bitstream/123456789/15767/1/MarcionilaOF.pdf7929f8f8aee297af940f4df074b1c3bbMD51TEXTMarcionilaOF.pdf.txtMarcionilaOF.pdf.txtExtracted texttext/plain221788https://repositorio.ufrn.br/bitstream/123456789/15767/6/MarcionilaOF.pdf.txt415cc7b3f738e4cdb055ff6dd0991cf7MD56THUMBNAILMarcionilaOF.pdf.jpgMarcionilaOF.pdf.jpgIM Thumbnailimage/jpeg4235https://repositorio.ufrn.br/bitstream/123456789/15767/7/MarcionilaOF.pdf.jpgd97cf0bc59647ae58ef7c11dfb0159b3MD57123456789/157672017-11-02 03:06:23.804oai:https://repositorio.ufrn.br:123456789/15767Repositório de PublicaçõesPUBhttp://repositorio.ufrn.br/oai/opendoar:2017-11-02T06:06:23Repositório Institucional da UFRN - Universidade Federal do Rio Grande do Norte (UFRN)false
dc.title.por.fl_str_mv Purificação da glicerina bruta obtida a partir da transesterificação do óleo de algodão
Purificação da glicerina bruta obtida a partir da transesterificação do óleo de algodão
title Purificação da glicerina bruta obtida a partir da transesterificação do óleo de algodão
spellingShingle Purificação da glicerina bruta obtida a partir da transesterificação do óleo de algodão
Ferreira, Marcionila de Oliveira
Purificação da glicerina
troca iônica
adsorção
Glycerin purification
ion exchange
adsorption
CNPQ::ENGENHARIAS::ENGENHARIA QUIMICA
title_short Purificação da glicerina bruta obtida a partir da transesterificação do óleo de algodão
title_full Purificação da glicerina bruta obtida a partir da transesterificação do óleo de algodão
title_fullStr Purificação da glicerina bruta obtida a partir da transesterificação do óleo de algodão
title_full_unstemmed Purificação da glicerina bruta obtida a partir da transesterificação do óleo de algodão
title_sort Purificação da glicerina bruta obtida a partir da transesterificação do óleo de algodão
author Ferreira, Marcionila de Oliveira
author_facet Ferreira, Marcionila de Oliveira
author_role author
dc.contributor.authorID.por.fl_str_mv
dc.contributor.authorLattes.por.fl_str_mv http://lattes.cnpq.br/0362693118434408
dc.contributor.advisorID.por.fl_str_mv
dc.contributor.advisorLattes.por.fl_str_mv http://lattes.cnpq.br/8055289812908100
dc.contributor.advisor-co1ID.por.fl_str_mv
dc.contributor.referees1.pt_BR.fl_str_mv Oliveira, Humberto Neves Maia de
dc.contributor.referees1ID.por.fl_str_mv
dc.contributor.referees1Lattes.por.fl_str_mv http://lattes.cnpq.br/7302633941782540
dc.contributor.referees2.pt_BR.fl_str_mv Oliveira, Jackson Araújo de
dc.contributor.referees2ID.por.fl_str_mv
dc.contributor.referees2Lattes.por.fl_str_mv http://lattes.cnpq.br/5058617634570704
dc.contributor.author.fl_str_mv Ferreira, Marcionila de Oliveira
dc.contributor.advisor-co1.fl_str_mv Sousa, Elisa Maria Bittencourt Dutra de
dc.contributor.advisor-co1Lattes.fl_str_mv http://buscatextual.cnpq.br/buscatextual/visualizacv.do?id=K4787769D1
dc.contributor.advisor1.fl_str_mv Pereira, Camila Gambini
contributor_str_mv Sousa, Elisa Maria Bittencourt Dutra de
Pereira, Camila Gambini
dc.subject.por.fl_str_mv Purificação da glicerina
troca iônica
adsorção
topic Purificação da glicerina
troca iônica
adsorção
Glycerin purification
ion exchange
adsorption
CNPQ::ENGENHARIAS::ENGENHARIA QUIMICA
dc.subject.eng.fl_str_mv Glycerin purification
ion exchange
adsorption
dc.subject.cnpq.fl_str_mv CNPQ::ENGENHARIAS::ENGENHARIA QUIMICA
description The crude glycerine is a raw material that can be used in a wide variety of products. Even with all the impurities inherent in the process of being obtained, the crude glycerin is already in a marketable product. However, the market is much more favorable to the commercialization of purified glycerine. The glycerin is a byproduct gotten from the process of transesterification of waste oils and fats in the production of biodiesel. More recently, the deployment of the new Federal Law of Brazil, related to the implementation of energy resources, forces, from 2008, the increase of 2% biodiesel in diesel common with prospects for 5% (B5). Therefore, it is indispensable that new routes of purification as well as new markets are developed. The objective of this work was to purify, through ion exchange, the crude glycerin, obtained from the reaction of transesterification of cottonseed oil. The cottonseed oil was characterized as the fatty acid composition and physical-chemical properties. The process of ion exchange was conducted in batch. In this process were used strong cation, low anion resins and a mixed resin used to de-ionize water. The purified glycerin was characterized as the content of metals. Tests were performed with activated charcoal adsorption, and for this, it was made tests of time contact with coal as well as quantity of coal used. The time of activation, the amount of the activation solution, the contact time of the glycerol solution in resins, the amount and type of resin applied were evaluated. Considering the analysis made with activated charcoal, when the glycerin solution was treated using the resins individually it was observed that in the conditions for treatment with 10 g of resin, 5 hours of contact with each resin and 50 mL of glycerin solution, its conductivity decreased to a cationic resin, increased to the anionic resin and had a variable value with respect to resin mixed. In the treatment in series, there was a constant decrease in the conductivity of the solution of glycerin. Considering two types of treatment, in series and individually, the content of glycerol in glycerin pre-purified solution with the different resins varied from 12,46 to 29.51% (diluted solution). In analysis performed without the use of activated charcoal, the behavior of the conductivity of the solution of glycerin were similar to results for treatment with activated charcoal, both in series as individually. The solution of glycerin pre-purified had a glycerol content varying from 8.3 to 25.7% (diluted solution). In relation to pH, it had a behavior in accordance with the expected: acid for the glycerin solution treated with cationic resin, basic when the glycerin solution was treated with the anionic resin and neutral when treated with the mixed resin, independent of the kind of procedure used (with or without coal, resins individually or in series). In relation to the color of the glycerin pre-purified solution, the resin that showed the best result was the anionic (colorless), however this does not mean that the solution is more in pure glycerol. The chromatographic analysis of the solutions obtained after the passage through the resins indicated that the treatment was effective by the presence of only one component (glycerol), not considering the solvent of the analysis
publishDate 2009
dc.date.available.fl_str_mv 2009-07-13
2014-12-17T15:01:18Z
dc.date.issued.fl_str_mv 2009-03-05
dc.date.accessioned.fl_str_mv 2014-12-17T15:01:18Z
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dc.identifier.citation.fl_str_mv FERREIRA, Marcionila de Oliveira. Purificação da glicerina bruta obtida a partir da transesterificação do óleo de algodão. 2009. 127 f. Dissertação (Mestrado em Pesquisa e Desenvolvimento de Tecnologias Regionais) - Universidade Federal do Rio Grande do Norte, Natal, 2009.
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identifier_str_mv FERREIRA, Marcionila de Oliveira. Purificação da glicerina bruta obtida a partir da transesterificação do óleo de algodão. 2009. 127 f. Dissertação (Mestrado em Pesquisa e Desenvolvimento de Tecnologias Regionais) - Universidade Federal do Rio Grande do Norte, Natal, 2009.
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