Kinetics for the biodiesel production from lauric acid over Keggin heteropolyacid loaded in silica framework
- Autores
- Gallego Villada, Luis A.; Alarcón Durango, Edwin Alexis; Palermo, Valeria; Vazquez, Patricia Graciela; Romanelli, Gustavo Pablo
- Año de publicación
- 2020
- Idioma
- inglés
- Tipo de recurso
- artículo
- Estado
- versión publicada
- Descripción
- Kinetic models were developed to describe the esterification reaction of lauric acid and ethanol over heterogeneous catalysts, which is a reaction of special interest in the biodiesel production. Vanadium Keggin heteropolyacid was included on a silica framework by sol–gel procedure, using different loadings. The synthesized materials were characterized by FT-IR, XRD, SEM, nitrogen adsorption/desorption isotherms, and potentiometric titration, and tested as solid catalysts in the esterification of lauric acid. Best performance was achieved with SiO2@20PMoV, which was used in the esterification of others fatty acid and alcohols. The reuse was successfully tested in five consecutive runs. Kinetic data using SiO2@20PMoV were obtained at different temperatures (48–78 °C), fatty acid:alcohol molar ratios (4 mmol of lauric acid and 2.5, 5, 10 and 15 mL of ethanol), and catalyst amounts (12.5, 25 and 50 mg). The best heterogeneous models were LH3 (surface reaction as rate-limiting step) and ER3 (desorption of ethyl laurate as rate-limiting step when the adsorbed reactant is lauric acid). The activation energies were 56.1 kJ mol−1 and 64.8 kJ mol−1, and the reaction rate constants at 78 °C were 0.2791 mol g−1 h−1 and 0.0768 mol g−1 h−1 for LH3 and ER3, respectively.
Fil: Gallego Villada, Luis A.. Universidad de Antioquia; Colombia
Fil: Alarcón Durango, Edwin Alexis. Universidad de Antioquia; Colombia
Fil: Palermo, Valeria. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - La Plata. Centro de Investigación y Desarrollo en Ciencias Aplicadas "Dr. Jorge J. Ronco". Universidad Nacional de la Plata. Facultad de Ciencias Exactas. Centro de Investigación y Desarrollo en Ciencias Aplicadas; Argentina
Fil: Vazquez, Patricia Graciela. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - La Plata. Centro de Investigación y Desarrollo en Ciencias Aplicadas "Dr. Jorge J. Ronco". Universidad Nacional de La Plata. Facultad de Ciencias Exactas. Centro de Investigación y Desarrollo en Ciencias Aplicadas; Argentina
Fil: Romanelli, Gustavo Pablo. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - La Plata. Centro de Investigación y Desarrollo en Ciencias Aplicadas "Dr. Jorge J. Ronco". Universidad Nacional de La Plata. Facultad de Ciencias Exactas. Centro de Investigación y Desarrollo en Ciencias Aplicadas; Argentina - Materia
-
BIODIESEL
ESTERIFICATION
HETEROGENEOUS CATALYSIS
KINETIC MODELING
LAURIC ACID
VANADIUM KEGGIN HETEROPOLYACID - Nivel de accesibilidad
- acceso abierto
- Condiciones de uso
- https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
- Repositorio
- Institución
- Consejo Nacional de Investigaciones Científicas y Técnicas
- OAI Identificador
- oai:ri.conicet.gov.ar:11336/167409
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Kinetics for the biodiesel production from lauric acid over Keggin heteropolyacid loaded in silica frameworkGallego Villada, Luis A.Alarcón Durango, Edwin AlexisPalermo, ValeriaVazquez, Patricia GracielaRomanelli, Gustavo PabloBIODIESELESTERIFICATIONHETEROGENEOUS CATALYSISKINETIC MODELINGLAURIC ACIDVANADIUM KEGGIN HETEROPOLYACIDhttps://purl.org/becyt/ford/2.4https://purl.org/becyt/ford/2Kinetic models were developed to describe the esterification reaction of lauric acid and ethanol over heterogeneous catalysts, which is a reaction of special interest in the biodiesel production. Vanadium Keggin heteropolyacid was included on a silica framework by sol–gel procedure, using different loadings. The synthesized materials were characterized by FT-IR, XRD, SEM, nitrogen adsorption/desorption isotherms, and potentiometric titration, and tested as solid catalysts in the esterification of lauric acid. Best performance was achieved with SiO2@20PMoV, which was used in the esterification of others fatty acid and alcohols. The reuse was successfully tested in five consecutive runs. Kinetic data using SiO2@20PMoV were obtained at different temperatures (48–78 °C), fatty acid:alcohol molar ratios (4 mmol of lauric acid and 2.5, 5, 10 and 15 mL of ethanol), and catalyst amounts (12.5, 25 and 50 mg). The best heterogeneous models were LH3 (surface reaction as rate-limiting step) and ER3 (desorption of ethyl laurate as rate-limiting step when the adsorbed reactant is lauric acid). The activation energies were 56.1 kJ mol−1 and 64.8 kJ mol−1, and the reaction rate constants at 78 °C were 0.2791 mol g−1 h−1 and 0.0768 mol g−1 h−1 for LH3 and ER3, respectively.Fil: Gallego Villada, Luis A.. Universidad de Antioquia; ColombiaFil: Alarcón Durango, Edwin Alexis. Universidad de Antioquia; ColombiaFil: Palermo, Valeria. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - La Plata. Centro de Investigación y Desarrollo en Ciencias Aplicadas "Dr. Jorge J. Ronco". Universidad Nacional de la Plata. Facultad de Ciencias Exactas. Centro de Investigación y Desarrollo en Ciencias Aplicadas; ArgentinaFil: Vazquez, Patricia Graciela. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - La Plata. Centro de Investigación y Desarrollo en Ciencias Aplicadas "Dr. Jorge J. Ronco". Universidad Nacional de La Plata. Facultad de Ciencias Exactas. Centro de Investigación y Desarrollo en Ciencias Aplicadas; ArgentinaFil: Romanelli, Gustavo Pablo. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - La Plata. Centro de Investigación y Desarrollo en Ciencias Aplicadas "Dr. Jorge J. Ronco". Universidad Nacional de La Plata. Facultad de Ciencias Exactas. Centro de Investigación y Desarrollo en Ciencias Aplicadas; ArgentinaElsevier2020-09-06info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionhttp://purl.org/coar/resource_type/c_6501info:ar-repo/semantics/articuloapplication/pdfapplication/pdfhttp://hdl.handle.net/11336/167409Gallego Villada, Luis A.; Alarcón Durango, Edwin Alexis; Palermo, Valeria; Vazquez, Patricia Graciela; Romanelli, Gustavo Pablo; Kinetics for the biodiesel production from lauric acid over Keggin heteropolyacid loaded in silica framework; Elsevier; Journal Of Industrial And Engineering Chemistry; 92; 6-9-2020; 109-1191226-086XCONICET DigitalCONICETenginfo:eu-repo/semantics/altIdentifier/doi/10.1016/j.jiec.2020.08.030info:eu-repo/semantics/altIdentifier/url/https://www.sciencedirect.com/science/article/pii/S1226086X20303920info:eu-repo/semantics/openAccesshttps://creativecommons.org/licenses/by-nc-sa/2.5/ar/reponame:CONICET Digital (CONICET)instname:Consejo Nacional de Investigaciones Científicas y Técnicas2025-09-29T10:06:35Zoai:ri.conicet.gov.ar:11336/167409instacron:CONICETInstitucionalhttp://ri.conicet.gov.ar/Organismo científico-tecnológicoNo correspondehttp://ri.conicet.gov.ar/oai/requestdasensio@conicet.gov.ar; lcarlino@conicet.gov.arArgentinaNo correspondeNo correspondeNo correspondeopendoar:34982025-09-29 10:06:35.914CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicasfalse |
dc.title.none.fl_str_mv |
Kinetics for the biodiesel production from lauric acid over Keggin heteropolyacid loaded in silica framework |
title |
Kinetics for the biodiesel production from lauric acid over Keggin heteropolyacid loaded in silica framework |
spellingShingle |
Kinetics for the biodiesel production from lauric acid over Keggin heteropolyacid loaded in silica framework Gallego Villada, Luis A. BIODIESEL ESTERIFICATION HETEROGENEOUS CATALYSIS KINETIC MODELING LAURIC ACID VANADIUM KEGGIN HETEROPOLYACID |
title_short |
Kinetics for the biodiesel production from lauric acid over Keggin heteropolyacid loaded in silica framework |
title_full |
Kinetics for the biodiesel production from lauric acid over Keggin heteropolyacid loaded in silica framework |
title_fullStr |
Kinetics for the biodiesel production from lauric acid over Keggin heteropolyacid loaded in silica framework |
title_full_unstemmed |
Kinetics for the biodiesel production from lauric acid over Keggin heteropolyacid loaded in silica framework |
title_sort |
Kinetics for the biodiesel production from lauric acid over Keggin heteropolyacid loaded in silica framework |
dc.creator.none.fl_str_mv |
Gallego Villada, Luis A. Alarcón Durango, Edwin Alexis Palermo, Valeria Vazquez, Patricia Graciela Romanelli, Gustavo Pablo |
author |
Gallego Villada, Luis A. |
author_facet |
Gallego Villada, Luis A. Alarcón Durango, Edwin Alexis Palermo, Valeria Vazquez, Patricia Graciela Romanelli, Gustavo Pablo |
author_role |
author |
author2 |
Alarcón Durango, Edwin Alexis Palermo, Valeria Vazquez, Patricia Graciela Romanelli, Gustavo Pablo |
author2_role |
author author author author |
dc.subject.none.fl_str_mv |
BIODIESEL ESTERIFICATION HETEROGENEOUS CATALYSIS KINETIC MODELING LAURIC ACID VANADIUM KEGGIN HETEROPOLYACID |
topic |
BIODIESEL ESTERIFICATION HETEROGENEOUS CATALYSIS KINETIC MODELING LAURIC ACID VANADIUM KEGGIN HETEROPOLYACID |
purl_subject.fl_str_mv |
https://purl.org/becyt/ford/2.4 https://purl.org/becyt/ford/2 |
dc.description.none.fl_txt_mv |
Kinetic models were developed to describe the esterification reaction of lauric acid and ethanol over heterogeneous catalysts, which is a reaction of special interest in the biodiesel production. Vanadium Keggin heteropolyacid was included on a silica framework by sol–gel procedure, using different loadings. The synthesized materials were characterized by FT-IR, XRD, SEM, nitrogen adsorption/desorption isotherms, and potentiometric titration, and tested as solid catalysts in the esterification of lauric acid. Best performance was achieved with SiO2@20PMoV, which was used in the esterification of others fatty acid and alcohols. The reuse was successfully tested in five consecutive runs. Kinetic data using SiO2@20PMoV were obtained at different temperatures (48–78 °C), fatty acid:alcohol molar ratios (4 mmol of lauric acid and 2.5, 5, 10 and 15 mL of ethanol), and catalyst amounts (12.5, 25 and 50 mg). The best heterogeneous models were LH3 (surface reaction as rate-limiting step) and ER3 (desorption of ethyl laurate as rate-limiting step when the adsorbed reactant is lauric acid). The activation energies were 56.1 kJ mol−1 and 64.8 kJ mol−1, and the reaction rate constants at 78 °C were 0.2791 mol g−1 h−1 and 0.0768 mol g−1 h−1 for LH3 and ER3, respectively. Fil: Gallego Villada, Luis A.. Universidad de Antioquia; Colombia Fil: Alarcón Durango, Edwin Alexis. Universidad de Antioquia; Colombia Fil: Palermo, Valeria. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - La Plata. Centro de Investigación y Desarrollo en Ciencias Aplicadas "Dr. Jorge J. Ronco". Universidad Nacional de la Plata. Facultad de Ciencias Exactas. Centro de Investigación y Desarrollo en Ciencias Aplicadas; Argentina Fil: Vazquez, Patricia Graciela. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - La Plata. Centro de Investigación y Desarrollo en Ciencias Aplicadas "Dr. Jorge J. Ronco". Universidad Nacional de La Plata. Facultad de Ciencias Exactas. Centro de Investigación y Desarrollo en Ciencias Aplicadas; Argentina Fil: Romanelli, Gustavo Pablo. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - La Plata. Centro de Investigación y Desarrollo en Ciencias Aplicadas "Dr. Jorge J. Ronco". Universidad Nacional de La Plata. Facultad de Ciencias Exactas. Centro de Investigación y Desarrollo en Ciencias Aplicadas; Argentina |
description |
Kinetic models were developed to describe the esterification reaction of lauric acid and ethanol over heterogeneous catalysts, which is a reaction of special interest in the biodiesel production. Vanadium Keggin heteropolyacid was included on a silica framework by sol–gel procedure, using different loadings. The synthesized materials were characterized by FT-IR, XRD, SEM, nitrogen adsorption/desorption isotherms, and potentiometric titration, and tested as solid catalysts in the esterification of lauric acid. Best performance was achieved with SiO2@20PMoV, which was used in the esterification of others fatty acid and alcohols. The reuse was successfully tested in five consecutive runs. Kinetic data using SiO2@20PMoV were obtained at different temperatures (48–78 °C), fatty acid:alcohol molar ratios (4 mmol of lauric acid and 2.5, 5, 10 and 15 mL of ethanol), and catalyst amounts (12.5, 25 and 50 mg). The best heterogeneous models were LH3 (surface reaction as rate-limiting step) and ER3 (desorption of ethyl laurate as rate-limiting step when the adsorbed reactant is lauric acid). The activation energies were 56.1 kJ mol−1 and 64.8 kJ mol−1, and the reaction rate constants at 78 °C were 0.2791 mol g−1 h−1 and 0.0768 mol g−1 h−1 for LH3 and ER3, respectively. |
publishDate |
2020 |
dc.date.none.fl_str_mv |
2020-09-06 |
dc.type.none.fl_str_mv |
info:eu-repo/semantics/article info:eu-repo/semantics/publishedVersion http://purl.org/coar/resource_type/c_6501 info:ar-repo/semantics/articulo |
format |
article |
status_str |
publishedVersion |
dc.identifier.none.fl_str_mv |
http://hdl.handle.net/11336/167409 Gallego Villada, Luis A.; Alarcón Durango, Edwin Alexis; Palermo, Valeria; Vazquez, Patricia Graciela; Romanelli, Gustavo Pablo; Kinetics for the biodiesel production from lauric acid over Keggin heteropolyacid loaded in silica framework; Elsevier; Journal Of Industrial And Engineering Chemistry; 92; 6-9-2020; 109-119 1226-086X CONICET Digital CONICET |
url |
http://hdl.handle.net/11336/167409 |
identifier_str_mv |
Gallego Villada, Luis A.; Alarcón Durango, Edwin Alexis; Palermo, Valeria; Vazquez, Patricia Graciela; Romanelli, Gustavo Pablo; Kinetics for the biodiesel production from lauric acid over Keggin heteropolyacid loaded in silica framework; Elsevier; Journal Of Industrial And Engineering Chemistry; 92; 6-9-2020; 109-119 1226-086X CONICET Digital CONICET |
dc.language.none.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
info:eu-repo/semantics/altIdentifier/doi/10.1016/j.jiec.2020.08.030 info:eu-repo/semantics/altIdentifier/url/https://www.sciencedirect.com/science/article/pii/S1226086X20303920 |
dc.rights.none.fl_str_mv |
info:eu-repo/semantics/openAccess https://creativecommons.org/licenses/by-nc-sa/2.5/ar/ |
eu_rights_str_mv |
openAccess |
rights_invalid_str_mv |
https://creativecommons.org/licenses/by-nc-sa/2.5/ar/ |
dc.format.none.fl_str_mv |
application/pdf application/pdf |
dc.publisher.none.fl_str_mv |
Elsevier |
publisher.none.fl_str_mv |
Elsevier |
dc.source.none.fl_str_mv |
reponame:CONICET Digital (CONICET) instname:Consejo Nacional de Investigaciones Científicas y Técnicas |
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CONICET Digital (CONICET) |
collection |
CONICET Digital (CONICET) |
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Consejo Nacional de Investigaciones Científicas y Técnicas |
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CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicas |
repository.mail.fl_str_mv |
dasensio@conicet.gov.ar; lcarlino@conicet.gov.ar |
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1844613915818852352 |
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13.070432 |