Show simple item record

dc.creatorPérez, Omar
dc.creatorMiño Valdés, Juan Esteban
dc.creatorGarcía, Agustín
dc.creatorGonzález Suárez, Erenio
dc.date.accessioned2024-04-18T13:21:40Z
dc.date.available2024-04-18T13:21:40Z
dc.date.issued2019-03-06
dc.identifier.citationPérez, O., Miño Valdes, J. E., García, A., González, E. (2019). Fermentative kinetic modeling for protein biomass from sugar diversification. The Current Trends in Biomedical Engineering & Biosciences. California : Juniper Publishers, 18(5), p. 5.es_AR
dc.identifier.issn2572-1151
dc.identifier.otherCCPI-FI-A-044
dc.identifier.other24505
dc.identifier.urihttps://hdl.handle.net/20.500.12219/5263
dc.descriptionFil: Pérez, Omar. Universidad Central Marta Abreu de Las Villas; Cuba.es_AR
dc.descriptionFil: Miño Valdes, Juan Esteban. Universidad Nacional de Misiones. Facultad de Ingeniería. Departamento de Ingeniería Industrial; Argentina.es_AR
dc.descriptionFil: García, Agustín. Universidad Central Marta Abreu de Las Villas; Cuba.es_AR
dc.descriptionFil: González, Erenio. Universidad Central Marta Abreu de Las Villas; Cuba.es_AR
dc.description.abstractAn analysis of the models proposed in the scientific literature is carried out to describe the kinetics of fermentation from a substrate conformed by cane juice and supplemented with final honey and nutrients that are inoculated with autochthonous yeasts of the medium. It is proposed the adjustment of the models through the interactive simulation of processes with minimum integral error of the sums of the differences between the experimental values and those predicted by the models. Initial total reducing sugars concentrations of 45 and 62 g/L were considered maintaining the pH between 4.4 and 5.2 and the temperature at 36 C. The best adjustment to the experimental values was obtained for the free inhibition model of Teisiser, while the Monod model presents deficiencies to describe the first and last part of the growth curve. The parameters of Teiissier at S0=45 g/L are μm= 0,21 h-1 and KS = 11,21 g/L while at S0=62 g/L are μm= 0,25 h-1 and KS = 23,2 g/L. As a result of the simulation it was determined that there are no significant effects of inhibition by substrate or product and that the Malthos model of cell growth accurately describes this process.es_AR
dc.formatapplication/pdf
dc.format.extent318 KB
dc.language.isoenges_AR
dc.publisherJuniper Publishersen
dc.relationinfo:eu-repo/semantics/altIdentifier/doi/10.19080/CTBEB.2019.18.555998
dc.relationinfo:eu-repo/semantics/altIdentifier/urn/https://juniperpublishers.com/ctbeb/CTBEB.MS.ID.555998.php
dc.rightsinfo:eu-repo/semantics/openAccess
dc.subjectKineticsen
dc.subjectModelsen
dc.subjectFermentationen
dc.subjectProtein biomassen
dc.subjectSugar caneen
dc.titleFermentative kinetic modeling for protein biomass from sugar diversificationen
dc.typeinfo:eu-repo/semantics/article
dc.typeinfo:ar-repo/semantics/artículo
dc.typeinfo:eu-repo/semantics/publishedVersion


Files in this item

Thumbnail
Thumbnail

This item appears in the following Collection(s)

Show simple item record