Kinetics for the biodiesel production from lauric acid over Keggin heteropolyacid loaded in silica framework

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...

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Authors: Gallego Villada, Luis A., Alarcón Durango, Edwin Alexis, Palermo, Valeria, Vazquez, Patricia Graciela, Romanelli, Gustavo Pablo
Format: article
Status:Published version
Publication Date:2020
Country:Argentina
Institution:Consejo Nacional de Investigaciones Científicas y Técnicas
Repository:CONICET Digital (CONICET)
Language:English
OAI Identifier:oai:ri.conicet.gov.ar:11336/167409
Online Access:http://hdl.handle.net/11336/167409
Access Level:Open access
Keyword:BIODIESEL
ESTERIFICATION
HETEROGENEOUS CATALYSIS
KINETIC MODELING
LAURIC ACID
VANADIUM KEGGIN HETEROPOLYACID
https://purl.org/becyt/ford/2.4
https://purl.org/becyt/ford/2
id AR_88ea3e01b3f5486a18fc67e66bf0b66a
oai_identifier_str oai:ri.conicet.gov.ar:11336/167409
network_acronym_str AR
network_name_str Argentina
repository_id_str
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
https://purl.org/becyt/ford/2.4
https://purl.org/becyt/ford/2
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
https://purl.org/becyt/ford/2.4
https://purl.org/becyt/ford/2
topic BIODIESEL
ESTERIFICATION
HETEROGENEOUS CATALYSIS
KINETIC MODELING
LAURIC ACID
VANADIUM KEGGIN HETEROPOLYACID
https://purl.org/becyt/ford/2.4
https://purl.org/becyt/ford/2
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
instname_str Consejo Nacional de Investigaciones Científicas y Técnicas
reponame_str CONICET Digital (CONICET)
collection CONICET Digital (CONICET)
repository.name.fl_str_mv CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicas
repository.mail.fl_str_mv dasensio@conicet.gov.ar; lcarlino@conicet.gov.ar
_version_ 1799195631810510848
spelling 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 Técnicas2024-05-08T13:58:37Zoai: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:34982024-05-08 13:58:37.992CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicasfalse
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