Effect of operating variables and kinetics of the lipase catalyzed transesterification of ethylene carbonate and glycerol
- Autores
- Gutierrez Lazaro, Ana; Velasco, Daniel; Boldrini, Diego Emmanuel; Yustos, Pedro; Esteban, Jesús; Ladero, Miguel
- Año de publicación
- 2018
- Idioma
- inglés
- Tipo de recurso
- artículo
- Estado
- versión publicada
- Descripción
- Glycerol carbonate (GC) is a value-added product originating from the valorization of widely available glycerol (Gly), a side stream from the production of biodiesel. Here we approach the production of this chemical comparing two reactions based on the transesterification of Gly with dimethyl carbonate (DMC) and ethylene carbonate (EC). For the former reaction, it was observed that the free enzyme CALB (lipase B from Candida antarctica) gave the best results, whereas for the latter, Eversa Transform (a genetic modification of Thermomyces lanuginosus lipase) performed better than the rest. With the selected catalysts, their immobilized analogous enzymes Novozym 435 and Lypozyme TL IM, respectively, were also tested. Observing that the yields for the reaction with EC were significantly faster, other operating variables were evaluated, resulting the best performance using a closed system, tert-butanol as solvent, a concentration of enzyme Eversa Transform of 3 % w/w, a molar excess of EC:Gly of 9:1 and a temperature of 60 C. Finally, several runs were conducted at different temperatures and molar ratios of EC:Gly, fitting a kinetic model to all experimental data for the reaction catalyzed with Eversa Transform. This model included the bimolecular transesterification reaction of Gly and EC catalyzed by the lipase and a reversible ring-opening polymerization of EC.
Fil: Gutierrez Lazaro, Ana. Complutense University of Madrid; España
Fil: Velasco, Daniel. Complutense University of Madrid; España
Fil: Boldrini, Diego Emmanuel. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina
Fil: Yustos, Pedro. Complutense University of Madrid; España
Fil: Esteban, Jesús. Max Planck Institute for Chemical Energy Conversion. Molecular Catalysis Division; Alemania
Fil: Ladero, Miguel. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina - Materia
-
EVERSA TRANSFORM 2.0
GLYCEROL
GLYCEROL CARBONATE
KINETIC MODEL
LIPOZYME TL 100 L
NOVOZYM 435 - Nivel de accesibilidad
- acceso abierto
- Condiciones de uso
- https://creativecommons.org/licenses/by/2.5/ar/
- Repositorio
.jpg)
- Institución
- Consejo Nacional de Investigaciones Científicas y Técnicas
- OAI Identificador
- oai:ri.conicet.gov.ar:11336/90798
Ver los metadatos del registro completo
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Effect of operating variables and kinetics of the lipase catalyzed transesterification of ethylene carbonate and glycerolGutierrez Lazaro, AnaVelasco, DanielBoldrini, Diego EmmanuelYustos, PedroEsteban, JesúsLadero, MiguelEVERSA TRANSFORM 2.0GLYCEROLGLYCEROL CARBONATEKINETIC MODELLIPOZYME TL 100 LNOVOZYM 435https://purl.org/becyt/ford/2.4https://purl.org/becyt/ford/2Glycerol carbonate (GC) is a value-added product originating from the valorization of widely available glycerol (Gly), a side stream from the production of biodiesel. Here we approach the production of this chemical comparing two reactions based on the transesterification of Gly with dimethyl carbonate (DMC) and ethylene carbonate (EC). For the former reaction, it was observed that the free enzyme CALB (lipase B from Candida antarctica) gave the best results, whereas for the latter, Eversa Transform (a genetic modification of Thermomyces lanuginosus lipase) performed better than the rest. With the selected catalysts, their immobilized analogous enzymes Novozym 435 and Lypozyme TL IM, respectively, were also tested. Observing that the yields for the reaction with EC were significantly faster, other operating variables were evaluated, resulting the best performance using a closed system, tert-butanol as solvent, a concentration of enzyme Eversa Transform of 3 % w/w, a molar excess of EC:Gly of 9:1 and a temperature of 60 C. Finally, several runs were conducted at different temperatures and molar ratios of EC:Gly, fitting a kinetic model to all experimental data for the reaction catalyzed with Eversa Transform. This model included the bimolecular transesterification reaction of Gly and EC catalyzed by the lipase and a reversible ring-opening polymerization of EC.Fil: Gutierrez Lazaro, Ana. Complutense University of Madrid; EspañaFil: Velasco, Daniel. Complutense University of Madrid; EspañaFil: Boldrini, Diego Emmanuel. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; ArgentinaFil: Yustos, Pedro. Complutense University of Madrid; EspañaFil: Esteban, Jesús. Max Planck Institute for Chemical Energy Conversion. Molecular Catalysis Division; AlemaniaFil: Ladero, Miguel. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; ArgentinaMDPI AG2018-09-05info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionhttp://purl.org/coar/resource_type/c_6501info:ar-repo/semantics/articuloapplication/pdfapplication/pdfhttp://hdl.handle.net/11336/90798Gutierrez Lazaro, Ana; Velasco, Daniel; Boldrini, Diego Emmanuel; Yustos, Pedro; Esteban, Jesús; et al.; Effect of operating variables and kinetics of the lipase catalyzed transesterification of ethylene carbonate and glycerol; MDPI AG; Fermentation; 4; 3; 5-9-2018; 1-142311-5637CONICET DigitalCONICETenginfo:eu-repo/semantics/altIdentifier/url/https://www.mdpi.com/2311-5637/4/3/75info:eu-repo/semantics/altIdentifier/doi/10.3390/fermentation4030075info:eu-repo/semantics/openAccesshttps://creativecommons.org/licenses/by/2.5/ar/reponame:CONICET Digital (CONICET)instname:Consejo Nacional de Investigaciones Científicas y Técnicas2025-12-23T14:47:25Zoai:ri.conicet.gov.ar:11336/90798instacron: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:34982025-12-23 14:47:25.556CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicasfalse |
| dc.title.none.fl_str_mv |
Effect of operating variables and kinetics of the lipase catalyzed transesterification of ethylene carbonate and glycerol |
| title |
Effect of operating variables and kinetics of the lipase catalyzed transesterification of ethylene carbonate and glycerol |
| spellingShingle |
Effect of operating variables and kinetics of the lipase catalyzed transesterification of ethylene carbonate and glycerol Gutierrez Lazaro, Ana EVERSA TRANSFORM 2.0 GLYCEROL GLYCEROL CARBONATE KINETIC MODEL LIPOZYME TL 100 L NOVOZYM 435 |
| title_short |
Effect of operating variables and kinetics of the lipase catalyzed transesterification of ethylene carbonate and glycerol |
| title_full |
Effect of operating variables and kinetics of the lipase catalyzed transesterification of ethylene carbonate and glycerol |
| title_fullStr |
Effect of operating variables and kinetics of the lipase catalyzed transesterification of ethylene carbonate and glycerol |
| title_full_unstemmed |
Effect of operating variables and kinetics of the lipase catalyzed transesterification of ethylene carbonate and glycerol |
| title_sort |
Effect of operating variables and kinetics of the lipase catalyzed transesterification of ethylene carbonate and glycerol |
| dc.creator.none.fl_str_mv |
Gutierrez Lazaro, Ana Velasco, Daniel Boldrini, Diego Emmanuel Yustos, Pedro Esteban, Jesús Ladero, Miguel |
| author |
Gutierrez Lazaro, Ana |
| author_facet |
Gutierrez Lazaro, Ana Velasco, Daniel Boldrini, Diego Emmanuel Yustos, Pedro Esteban, Jesús Ladero, Miguel |
| author_role |
author |
| author2 |
Velasco, Daniel Boldrini, Diego Emmanuel Yustos, Pedro Esteban, Jesús Ladero, Miguel |
| author2_role |
author author author author author |
| dc.subject.none.fl_str_mv |
EVERSA TRANSFORM 2.0 GLYCEROL GLYCEROL CARBONATE KINETIC MODEL LIPOZYME TL 100 L NOVOZYM 435 |
| topic |
EVERSA TRANSFORM 2.0 GLYCEROL GLYCEROL CARBONATE KINETIC MODEL LIPOZYME TL 100 L NOVOZYM 435 |
| purl_subject.fl_str_mv |
https://purl.org/becyt/ford/2.4 https://purl.org/becyt/ford/2 |
| dc.description.none.fl_txt_mv |
Glycerol carbonate (GC) is a value-added product originating from the valorization of widely available glycerol (Gly), a side stream from the production of biodiesel. Here we approach the production of this chemical comparing two reactions based on the transesterification of Gly with dimethyl carbonate (DMC) and ethylene carbonate (EC). For the former reaction, it was observed that the free enzyme CALB (lipase B from Candida antarctica) gave the best results, whereas for the latter, Eversa Transform (a genetic modification of Thermomyces lanuginosus lipase) performed better than the rest. With the selected catalysts, their immobilized analogous enzymes Novozym 435 and Lypozyme TL IM, respectively, were also tested. Observing that the yields for the reaction with EC were significantly faster, other operating variables were evaluated, resulting the best performance using a closed system, tert-butanol as solvent, a concentration of enzyme Eversa Transform of 3 % w/w, a molar excess of EC:Gly of 9:1 and a temperature of 60 C. Finally, several runs were conducted at different temperatures and molar ratios of EC:Gly, fitting a kinetic model to all experimental data for the reaction catalyzed with Eversa Transform. This model included the bimolecular transesterification reaction of Gly and EC catalyzed by the lipase and a reversible ring-opening polymerization of EC. Fil: Gutierrez Lazaro, Ana. Complutense University of Madrid; España Fil: Velasco, Daniel. Complutense University of Madrid; España Fil: Boldrini, Diego Emmanuel. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina Fil: Yustos, Pedro. Complutense University of Madrid; España Fil: Esteban, Jesús. Max Planck Institute for Chemical Energy Conversion. Molecular Catalysis Division; Alemania Fil: Ladero, Miguel. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina |
| description |
Glycerol carbonate (GC) is a value-added product originating from the valorization of widely available glycerol (Gly), a side stream from the production of biodiesel. Here we approach the production of this chemical comparing two reactions based on the transesterification of Gly with dimethyl carbonate (DMC) and ethylene carbonate (EC). For the former reaction, it was observed that the free enzyme CALB (lipase B from Candida antarctica) gave the best results, whereas for the latter, Eversa Transform (a genetic modification of Thermomyces lanuginosus lipase) performed better than the rest. With the selected catalysts, their immobilized analogous enzymes Novozym 435 and Lypozyme TL IM, respectively, were also tested. Observing that the yields for the reaction with EC were significantly faster, other operating variables were evaluated, resulting the best performance using a closed system, tert-butanol as solvent, a concentration of enzyme Eversa Transform of 3 % w/w, a molar excess of EC:Gly of 9:1 and a temperature of 60 C. Finally, several runs were conducted at different temperatures and molar ratios of EC:Gly, fitting a kinetic model to all experimental data for the reaction catalyzed with Eversa Transform. This model included the bimolecular transesterification reaction of Gly and EC catalyzed by the lipase and a reversible ring-opening polymerization of EC. |
| publishDate |
2018 |
| dc.date.none.fl_str_mv |
2018-09-05 |
| 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 |
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article |
| status_str |
publishedVersion |
| dc.identifier.none.fl_str_mv |
http://hdl.handle.net/11336/90798 Gutierrez Lazaro, Ana; Velasco, Daniel; Boldrini, Diego Emmanuel; Yustos, Pedro; Esteban, Jesús; et al.; Effect of operating variables and kinetics of the lipase catalyzed transesterification of ethylene carbonate and glycerol; MDPI AG; Fermentation; 4; 3; 5-9-2018; 1-14 2311-5637 CONICET Digital CONICET |
| url |
http://hdl.handle.net/11336/90798 |
| identifier_str_mv |
Gutierrez Lazaro, Ana; Velasco, Daniel; Boldrini, Diego Emmanuel; Yustos, Pedro; Esteban, Jesús; et al.; Effect of operating variables and kinetics of the lipase catalyzed transesterification of ethylene carbonate and glycerol; MDPI AG; Fermentation; 4; 3; 5-9-2018; 1-14 2311-5637 CONICET Digital CONICET |
| dc.language.none.fl_str_mv |
eng |
| language |
eng |
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info:eu-repo/semantics/altIdentifier/url/https://www.mdpi.com/2311-5637/4/3/75 info:eu-repo/semantics/altIdentifier/doi/10.3390/fermentation4030075 |
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info:eu-repo/semantics/openAccess https://creativecommons.org/licenses/by/2.5/ar/ |
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openAccess |
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https://creativecommons.org/licenses/by/2.5/ar/ |
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application/pdf application/pdf |
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MDPI AG |
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MDPI AG |
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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 |
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dasensio@conicet.gov.ar; lcarlino@conicet.gov.ar |
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