Influence of mono-hydrogenation of C5 cut on the synthesis of TAME using Amberlyst 15
Autor(a) principal: | |
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Data de Publicação: | 2008 |
Outros Autores: | , , |
Tipo de documento: | Artigo |
Idioma: | por |
Título da fonte: | Acta scientiarum. Technology (Online) |
Texto Completo: | http://www.periodicos.uem.br/ojs/index.php/ActaSciTechnol/article/view/2773 |
Resumo: | TAME was synthesized in liquid phase from refinery C5 cut and methanol using Amberlyst 15 as catalyst. The C5 stream contains mainly mono-olefins and, in a less amount, a diolefin, which have a high gum formation tendency. The main purpose of this research was to evaluate the effect of mono-hydrogenation of C5 cut on TAME synthesis. The hydrogenation step was carried out at 80 oC and 10 kgf/cm2 of H2, using a 0.3% Pt/Al2O3 catalyst. It was observed that the diolefin was totally hydrogenated and olefins content was drastically reduced without any decrease of reactive isoamylenes content. The etherification was carried out in a 250 mL stirred batch reactor at temperatures ranging 50 - 90 oC, 10 kgf/cm2, and molar ratio of isoamylenes to methanol close to 1. Reaction products were analyzed by GC. Total conversion was similar for original and mono-hydrogenated feeds. However, the products obtained with the original cut presented foul odor and color, even at lower temperatures, characteristic of gum formation in the products. On the other hand, the product obtained from the mono-hydrogenated cut presents no foul odor and color. Therefore, mono-hydrogenation of the C5 cut is necessary to allow the addition of the produced TAME to gasoline blend |
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Influence of mono-hydrogenation of C5 cut on the synthesis of TAME using Amberlyst 15Influência da mono-hidrogenação da fração C5 na síntese do TAME usando Amberlyst 15 como catalisadorTAMEhidrogenaçãoAmberlyst 153.06.00.00-6 Engenharia QuímicaTAME was synthesized in liquid phase from refinery C5 cut and methanol using Amberlyst 15 as catalyst. The C5 stream contains mainly mono-olefins and, in a less amount, a diolefin, which have a high gum formation tendency. The main purpose of this research was to evaluate the effect of mono-hydrogenation of C5 cut on TAME synthesis. The hydrogenation step was carried out at 80 oC and 10 kgf/cm2 of H2, using a 0.3% Pt/Al2O3 catalyst. It was observed that the diolefin was totally hydrogenated and olefins content was drastically reduced without any decrease of reactive isoamylenes content. The etherification was carried out in a 250 mL stirred batch reactor at temperatures ranging 50 - 90 oC, 10 kgf/cm2, and molar ratio of isoamylenes to methanol close to 1. Reaction products were analyzed by GC. Total conversion was similar for original and mono-hydrogenated feeds. However, the products obtained with the original cut presented foul odor and color, even at lower temperatures, characteristic of gum formation in the products. On the other hand, the product obtained from the mono-hydrogenated cut presents no foul odor and color. Therefore, mono-hydrogenation of the C5 cut is necessary to allow the addition of the produced TAME to gasoline blendNo presente trabalho, foi estudada a síntese do TAME, em fase líquida, a partir de uma fração C5 e metanol, utilizando Amberlyst 15 como catalisador. A fração C5 utilizada possui uma diolefina, que tem uma alta tendência à formação de gomas e um alto teor de mono-olefinas. Deste modo, o objetivo deste trabalho foi avaliar o efeito da mono-hidrogenação da fração C5 na síntese do TAME. A hidrogenação foi feita a 80oC e 10 kgf/cm2 de H2, usando um catalisador 0,3% Pt/Al2O3. A diolefina foi totalmente hidrogenada e o teor de mono-olefinas significativamente reduzido sem um decréscimo apreciável no teor de isoamilenos reativos. A eterificação foi feita em um reator tipo batelada de 250 mL, com agitação magnética. A temperatura foi variada na faixa de 50 a 90oC, com uma pressão de 10 kgf/cm2 e razão molar isoamileno/metanol de aproximadamente um. Os produtos de reação foram analisados por cromatografia gasosa. A conversão total observada foi aproximadamente a mesma para o os cortes original e mono-hidrogenado. Entretanto, os produtos obtidos utilizando a fração C5 original apresentaram cheiro forte e coloração, mesmos para os testes a temperaturas mais baixas, que são características da formação de gomas. Por outro lado, quando a fração mono-hidrogenada foi usada na eterificação, o cheiro forte e coloração não foram observados. Portanto, a mono-hidrogenação da fração C5 contendo os isoamilenos reativos é necessária para que o TAME produzido na reação de eterificação possa ser adicionado à gasolinaUniversidade Estadual De Maringá2008-05-05info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionapplication/pdfhttp://www.periodicos.uem.br/ojs/index.php/ActaSciTechnol/article/view/277310.4025/actascitechnol.v23i0.2773Acta Scientiarum. Technology; Vol 23 (2001); 1415-1419Acta Scientiarum. Technology; v. 23 (2001); 1415-14191806-25631807-8664reponame:Acta scientiarum. Technology (Online)instname:Universidade Estadual de Maringá (UEM)instacron:UEMporhttp://www.periodicos.uem.br/ojs/index.php/ActaSciTechnol/article/view/2773/1835Gonçalves, Gilberto da CunhaGazola, Fernando CesarSimoes Dornellas de Barros, Maria AngelicaArroyo, Pedro Augustoinfo:eu-repo/semantics/openAccess2024-05-17T13:02:49Zoai:periodicos.uem.br/ojs:article/2773Revistahttps://www.periodicos.uem.br/ojs/index.php/ActaSciTechnol/indexPUBhttps://www.periodicos.uem.br/ojs/index.php/ActaSciTechnol/oai||actatech@uem.br1807-86641806-2563opendoar:2024-05-17T13:02:49Acta scientiarum. Technology (Online) - Universidade Estadual de Maringá (UEM)false |
dc.title.none.fl_str_mv |
Influence of mono-hydrogenation of C5 cut on the synthesis of TAME using Amberlyst 15 Influência da mono-hidrogenação da fração C5 na síntese do TAME usando Amberlyst 15 como catalisador |
title |
Influence of mono-hydrogenation of C5 cut on the synthesis of TAME using Amberlyst 15 |
spellingShingle |
Influence of mono-hydrogenation of C5 cut on the synthesis of TAME using Amberlyst 15 Gonçalves, Gilberto da Cunha TAME hidrogenação Amberlyst 15 3.06.00.00-6 Engenharia Química |
title_short |
Influence of mono-hydrogenation of C5 cut on the synthesis of TAME using Amberlyst 15 |
title_full |
Influence of mono-hydrogenation of C5 cut on the synthesis of TAME using Amberlyst 15 |
title_fullStr |
Influence of mono-hydrogenation of C5 cut on the synthesis of TAME using Amberlyst 15 |
title_full_unstemmed |
Influence of mono-hydrogenation of C5 cut on the synthesis of TAME using Amberlyst 15 |
title_sort |
Influence of mono-hydrogenation of C5 cut on the synthesis of TAME using Amberlyst 15 |
author |
Gonçalves, Gilberto da Cunha |
author_facet |
Gonçalves, Gilberto da Cunha Gazola, Fernando Cesar Simoes Dornellas de Barros, Maria Angelica Arroyo, Pedro Augusto |
author_role |
author |
author2 |
Gazola, Fernando Cesar Simoes Dornellas de Barros, Maria Angelica Arroyo, Pedro Augusto |
author2_role |
author author author |
dc.contributor.author.fl_str_mv |
Gonçalves, Gilberto da Cunha Gazola, Fernando Cesar Simoes Dornellas de Barros, Maria Angelica Arroyo, Pedro Augusto |
dc.subject.por.fl_str_mv |
TAME hidrogenação Amberlyst 15 3.06.00.00-6 Engenharia Química |
topic |
TAME hidrogenação Amberlyst 15 3.06.00.00-6 Engenharia Química |
description |
TAME was synthesized in liquid phase from refinery C5 cut and methanol using Amberlyst 15 as catalyst. The C5 stream contains mainly mono-olefins and, in a less amount, a diolefin, which have a high gum formation tendency. The main purpose of this research was to evaluate the effect of mono-hydrogenation of C5 cut on TAME synthesis. The hydrogenation step was carried out at 80 oC and 10 kgf/cm2 of H2, using a 0.3% Pt/Al2O3 catalyst. It was observed that the diolefin was totally hydrogenated and olefins content was drastically reduced without any decrease of reactive isoamylenes content. The etherification was carried out in a 250 mL stirred batch reactor at temperatures ranging 50 - 90 oC, 10 kgf/cm2, and molar ratio of isoamylenes to methanol close to 1. Reaction products were analyzed by GC. Total conversion was similar for original and mono-hydrogenated feeds. However, the products obtained with the original cut presented foul odor and color, even at lower temperatures, characteristic of gum formation in the products. On the other hand, the product obtained from the mono-hydrogenated cut presents no foul odor and color. Therefore, mono-hydrogenation of the C5 cut is necessary to allow the addition of the produced TAME to gasoline blend |
publishDate |
2008 |
dc.date.none.fl_str_mv |
2008-05-05 |
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 |
http://www.periodicos.uem.br/ojs/index.php/ActaSciTechnol/article/view/2773 10.4025/actascitechnol.v23i0.2773 |
url |
http://www.periodicos.uem.br/ojs/index.php/ActaSciTechnol/article/view/2773 |
identifier_str_mv |
10.4025/actascitechnol.v23i0.2773 |
dc.language.iso.fl_str_mv |
por |
language |
por |
dc.relation.none.fl_str_mv |
http://www.periodicos.uem.br/ojs/index.php/ActaSciTechnol/article/view/2773/1835 |
dc.rights.driver.fl_str_mv |
info:eu-repo/semantics/openAccess |
eu_rights_str_mv |
openAccess |
dc.format.none.fl_str_mv |
application/pdf |
dc.publisher.none.fl_str_mv |
Universidade Estadual De Maringá |
publisher.none.fl_str_mv |
Universidade Estadual De Maringá |
dc.source.none.fl_str_mv |
Acta Scientiarum. Technology; Vol 23 (2001); 1415-1419 Acta Scientiarum. Technology; v. 23 (2001); 1415-1419 1806-2563 1807-8664 reponame:Acta scientiarum. Technology (Online) instname:Universidade Estadual de Maringá (UEM) instacron:UEM |
instname_str |
Universidade Estadual de Maringá (UEM) |
instacron_str |
UEM |
institution |
UEM |
reponame_str |
Acta scientiarum. Technology (Online) |
collection |
Acta scientiarum. Technology (Online) |
repository.name.fl_str_mv |
Acta scientiarum. Technology (Online) - Universidade Estadual de Maringá (UEM) |
repository.mail.fl_str_mv |
||actatech@uem.br |
_version_ |
1799315332493475840 |