Mostrar el registro sencillo del ítem
Semi-continuous mechanochemical process for biodiesel production under heterogeneous catalysis using calcium diglyceroxide
dc.contributor.author | Malpartida-García, Irene | |
dc.contributor.author | Maireles-Torres, Pedro Jesús | |
dc.contributor.author | Vereda-Alonso, Carlos | |
dc.contributor.author | Rodríguez-Maroto, José Miguel | |
dc.contributor.author | Halloumi, Samy | |
dc.contributor.author | Lair, Valentin | |
dc.contributor.author | Thiel, Julien | |
dc.contributor.author | Lacoste, François | |
dc.date.accessioned | 2024-01-09T07:19:56Z | |
dc.date.available | 2024-01-09T07:19:56Z | |
dc.date.created | 2024 | |
dc.date.issued | 2020-05-26 | |
dc.identifier.citation | Malpartida, I., Maireles-Torres, P., Vereda, C., Rodríguez-Maroto, J. M., Halloumi, S., Lair, V., Thiel, J., & Lacoste, F. (2020). Semi-continuous mechanochemical process for biodiesel production under heterogeneous catalysis using calcium diglyceroxide. Renewable Energy, 159, 117–126. | es_ES |
dc.identifier.uri | https://hdl.handle.net/10630/28518 | |
dc.description.abstract | This work is aimed at the development of a semi-continuous mechanochemical process for biodiesel production and the subsequent valorization of glycerol, its by-product, via its conversion into calcium diglyceroxide using the same mechanochemical reactor. This basic solid catalyzes the methanolysis of vegetable oils. The implementation of a semi-continuous process allows both the preparation of the solid catalyst and the methanolysis process, overcoming the miscibility problems of methanol and oil. Thus, a biodiesel yield higher than 90% is reached using a methanol:oil molar ratio close to stoichiometric value and 1.5 wt.% catalyst, after passing through the reactor with a flow rate between 4 to 45 L/h. This new process for biodiesel production can easily be scaled up and applied to the conversion of used cooking oils, without any significant yield decrease. A cost study was also performed, demonstrating that this is more economical than the conventional batch stirring-based process. | es_ES |
dc.description.sponsorship | Deasyl: CONTRATO 806/41.5524_08.06.00.35.80 | es_ES |
dc.language.iso | eng | es_ES |
dc.publisher | Elsevier Ltd. | es_ES |
dc.rights | Attribution-NonCommercial-NoDerivatives 4.0 Internacional | * |
dc.rights.uri | http://creativecommons.org/licenses/by-nc-nd/4.0/ | * |
dc.subject | Energía de biomasa | es_ES |
dc.subject | Catálisis heterogénea | es_ES |
dc.subject | Glicerina | es_ES |
dc.subject.other | Calcium glyceroxide | es_ES |
dc.subject.other | Biodiesel | es_ES |
dc.subject.other | Heterogeneous catalysis | es_ES |
dc.subject.other | Mechanochemistry | es_ES |
dc.subject.other | Continuous flow | es_ES |
dc.subject.other | Mechanochemical process | es_ES |
dc.title | Semi-continuous mechanochemical process for biodiesel production under heterogeneous catalysis using calcium diglyceroxide | es_ES |
dc.type | journal article | es_ES |
dc.centro | Facultad de Ciencias | es_ES |
dc.identifier.doi | 10.1016/j.renene.2020.05.020 | |
dc.type.hasVersion | AM | es_ES |
dc.departamento | Química Inorgánica, Cristalografía y Mineralografía | |
dc.rights.accessRights | open access | es_ES |