Submitted by Jos? Henrique Henrique (jose.neves@ufvjm.edu.br) on 2017-06-02T20:34:08Z No. of bitstreams: 2 camila_diana_lima.pdf: 4383425 bytes, checksum: a00aa24c475acb8858df11e235a0c29c (MD5) license_rdf: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5) / Approved for entry into archive by Rodrigo Martins Cruz (rodrigo.cruz@ufvjm.edu.br) on 2017-06-14T19:40:25Z (GMT) No. of bitstreams: 2 camila_diana_lima.pdf: 4383425 bytes, checksum: a00aa24c475acb8858df11e235a0c29c (MD5) license_rdf: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5) / Made available in DSpace on 2017-06-14T19:40:25Z (GMT). No. of bitstreams: 2 camila_diana_lima.pdf: 4383425 bytes, checksum: a00aa24c475acb8858df11e235a0c29c (MD5) license_rdf: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5) Previous issue date: 2017 / O presente trabalho descreve o estudo de novas metodologias para obten??o de ?steres benz?licos e ?steres met?licos de ?cidos graxos (biodiesel) utilizando o NbCl5 s?lido e catalisadores heterog?neos ?cidos. No estudo, o NbCl5 s?lido foi utilizado como reagente, e nos outros m?todos foi empregado um catalisador de ni?bio enxertado em s?lica e um catalisador de grupos sulf?nicos imobilizado em s?lica. Nos processos heterog?neos a SiO2 (507 m2g-1, ?rea espec?fica) utilizada como suporte dos catalisadores, foi produzida a partir de areia constru??o e carbonato. O NbCl5 e os grupos ?SO3H foram imobilizados diretamente ? temperatura ambiente na SiO2, formando respectivamente o SiO2-Nb, com 412 m2g-1 de ?rea espec?fica e o SiO2-SO3H, com 115 m2g-1 de ?rea espec?fica. Nas esterifica??es utilizando NbCl5 s?lido foi determinado que para a obten??o de rendimentos razo?veis de ?steres de benz?licos (>85%) e ?steres met?licos (>70%) em rea??es a temperatura ambiente, a propor??o m?nima em moles de NbCl5:?lcool benz?lico deve ser 1,5:1,0 e para obten??o dos ?steres met?licos a propor??o de 1,5:6,0. Nas metodologias aplicando os catalisadores heterog?neos foi utilizada uma quantidade de 7% (m/m) do catalisador SiO2-SO3H para catalisar a esterifica??o de diferentes ?cidos carbox?licos com ?lcool benz?lico. E para as mesmas rea??es com o catalisador SiO2-Nb foi utilizada uma raz?o de 10% (m/m) do catalisador. Ambos os processos foram realizados sob refluxo na aus?ncia de um solvente; rendimentos muito semelhantes foram obtidos apesar do catalisador SiO2-SO3H possuir uma ?rea superficial muito menor que o catalisador SiO2-Nb. / Disserta??o (Mestrado) ? Programa de P?s-gradua??o em Biocombust?veis, Universidade Federal dos Vales do Jequitinhonha e Mucuri, 2017. / The current work describes the study of new methodologies for obtaining benzyl esters and methyl esters of fatty acids (biodiesel) using solid NbCl5 and heterogeneous acid catalysts. In this study, solid NbCl5 was used as a reagent, and in the other methods a silica grafted niobium catalyst and a sulphonic group catalyst immobilized on silica were used. In the heterogeneous processes the SiO2 (507 m2g-1, specific area) used as support of the catalysts, was produced from sand building and carbonate. The NbCl5 and the -SO3H groups were directly immobilized at room temperature in SiO2, forming respectively SiO2-Nb, with 412 m2g-1 of specific area and SiO2 -SO3H, with 115 m2g-1 of specific area. In the esterifications using solid NbCl5 it was determined that in order to obtain reasonable yields of benzyl esters (>85%) and methyl esters (>70%) in reactions at room temperature, the minimum mole ratio of NbCl5/benzyl alcohol should be 1,5:1,0 and in the obtainment of the methyl esters at a ratio of 1,5:6,0. In the methodologies applying the heterogeneous catalysts to an amount of 7% (w/w) of the catalyst SiO2 -SO3H to catalyze an esterification of different carboxylic acids with benzyl alcohol. Both processes were performed under reflux in the absence of a solvent; very similar yields were obtained although the SiO2-SO3H catalyst had a much lower surface area than the SiO2-Nb catalyst.