Kinetic modeling of batch bioethanol production from CCN-51 cocoa mucilage

dc.contributor.authorDelgado Noboa, Jorge Washington
dc.date.accessioned2021-10-29T13:51:52Z
dc.date.available2021-10-29T13:51:52Z
dc.date.issued2021
dc.description.abstractBackground: The aim of this study was the production of bioethanol generated during the fermentation of CCN-51 Cocoa mucilage with Saccharomyces cerevisiae yeast and the fitting of experimental data to the mathematical models: Logistic, modified Gompertz, and Andrews and Levenspiel. There are limited studies regarding the high energy potential of cocoa mucilage from Ecuador for bioethanol production as a gasoline additive. Currently, this by-product of the cocoa industry is considered as waste. Methods: Discontinuous fermentation was performed in a batch bioreactor under different conditions of pH, temperature and yeast concentration. During the reaction, bioethanol concentration, yeast and consumed substrate were evaluated by means of microdiffusion, dry weight by lyophilization and UV spectrophotometry, respectively. Significant Findings: The result of the final bioethanol concentration was 25.41 g/L at a temperature of 35 °C, pH of 4 and yeast concentration of 3 g/L. The models were fitted with determination coefficients greater than 0.9. From the results, the logistic model was used to describe yeast growth. Modified Gompertz model is considered appropriate for modeling bioethanol production. Both models fit the data adequately; however, Andrews and Levenspiel model, besides of the good adjustment, considered inhibition terms of the substrate and product.
dc.identifier.doi10.1016/j.jtice.2021.08.040
dc.identifier.issn1876-1070
dc.identifier.urihttp://dspace.ucuenca.edu.ec/handle/123456789/37182
dc.identifier.urihttps://doi.org/10.1016/j.jtice.2021.08.040
dc.language.isoes_ES
dc.sourceJournal of the Taiwan Institute of Chemical Engineers
dc.subjectAlcoholic fermentation
dc.titleKinetic modeling of batch bioethanol production from CCN-51 cocoa mucilage
dc.typeARTÍCULO
dc.ucuenca.afiliacionSoler, J., Universidad de Zaragoza, Zaragoza, España
dc.ucuenca.areaconocimientofrascatiamplio2. Ingeniería y Tecnología
dc.ucuenca.areaconocimientofrascatidetallado2.4.2 Ingeniería de Procesos Químicos
dc.ucuenca.areaconocimientofrascatiespecifico2.4 Ingeniería Química
dc.ucuenca.areaconocimientounescoamplio07 - Ingeniería, Industria y Construcción
dc.ucuenca.areaconocimientounescodetallado0711 - Ingeniería y Procesos Químicos
dc.ucuenca.areaconocimientounescoespecifico071 - Ingeniería y Profesiones Afines
dc.ucuenca.correspondenciaDelgado Noboa, Jorge Washington, jorge.delgado@ucuenca.edu.ec
dc.ucuenca.cuartilQ1
dc.ucuenca.factorimpacto0.99
dc.ucuenca.idautor0000-0002-8383-4996
dc.ucuenca.indicebibliograficoSCOPUS
dc.ucuenca.numerocitaciones0
dc.ucuenca.urifuentehttps://www.sciencedirect.com/journal/journal-of-the-taiwan-institute-of-chemical-engineers/vol/128/suppl/C
dc.ucuenca.versionVersión publicada
dc.ucuenca.volumenVolumen 128

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