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dc.contributor.author
Gutierrez Lazaro, Ana  
dc.contributor.author
Velasco, Daniel  
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Boldrini, Diego Emmanuel  
dc.contributor.author
Yustos, Pedro  
dc.contributor.author
Esteban, Jesús  
dc.contributor.author
Ladero, Miguel  
dc.date.available
2019-11-28T18:10:53Z  
dc.date.issued
2018-09-05  
dc.identifier.citation
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  
dc.identifier.issn
2311-5637  
dc.identifier.uri
http://hdl.handle.net/11336/90798  
dc.description.abstract
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.  
dc.format
application/pdf  
dc.language.iso
eng  
dc.publisher
MDPI AG  
dc.rights
info:eu-repo/semantics/openAccess  
dc.rights.uri
https://creativecommons.org/licenses/by/2.5/ar/  
dc.subject
EVERSA TRANSFORM 2.0  
dc.subject
GLYCEROL  
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GLYCEROL CARBONATE  
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KINETIC MODEL  
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LIPOZYME TL 100 L  
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NOVOZYM 435  
dc.subject.classification
Otras Ingeniería Química  
dc.subject.classification
Ingeniería Química  
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INGENIERÍAS Y TECNOLOGÍAS  
dc.title
Effect of operating variables and kinetics of the lipase catalyzed transesterification of ethylene carbonate and glycerol  
dc.type
info:eu-repo/semantics/article  
dc.type
info:ar-repo/semantics/artículo  
dc.type
info:eu-repo/semantics/publishedVersion  
dc.date.updated
2019-10-24T19:37:13Z  
dc.journal.volume
4  
dc.journal.number
3  
dc.journal.pagination
1-14  
dc.journal.pais
Suiza  
dc.journal.ciudad
Basilea  
dc.description.fil
Fil: Gutierrez Lazaro, Ana. Complutense University of Madrid; España  
dc.description.fil
Fil: Velasco, Daniel. Complutense University of Madrid; España  
dc.description.fil
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  
dc.description.fil
Fil: Yustos, Pedro. Complutense University of Madrid; España  
dc.description.fil
Fil: Esteban, Jesús. Max Planck Institute for Chemical Energy Conversion. Molecular Catalysis Division; Alemania  
dc.description.fil
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  
dc.journal.title
Fermentation  
dc.relation.alternativeid
info:eu-repo/semantics/altIdentifier/url/https://www.mdpi.com/2311-5637/4/3/75  
dc.relation.alternativeid
info:eu-repo/semantics/altIdentifier/doi/http://dx.doi.org/10.3390/fermentation4030075