Please use this identifier to cite or link to this item:
http://hdl.handle.net/10553/113841
DC Field | Value | Language |
---|---|---|
dc.contributor.author | Sosa Marco, Adriel | en_US |
dc.contributor.author | Ortega García, Juan Miguel | en_US |
dc.contributor.author | Fernández Suárez, Luis Jesús | en_US |
dc.contributor.author | Lorenzo Pérez, Beatriz | en_US |
dc.date.accessioned | 2022-02-21T08:29:46Z | - |
dc.date.available | 2022-02-21T08:29:46Z | - |
dc.date.issued | 2022 | en_US |
dc.identifier.issn | 1226-086X | en_US |
dc.identifier.other | Scopus | - |
dc.identifier.uri | http://hdl.handle.net/10553/113841 | - |
dc.description.abstract | A modelling methodology based on the precision-complexity binomial has been applied to a parametric model established for the Gibbs function, in order to achieve the best parameterization. This methodology is integrated into a multi-objective optimization method to describe, as accurately as possible, the real behaviour of a set of binary solutions of butyl butanoate-alkanes, for which several of their properties have been experimentally determined. The optimization is addressed with a genetic algorithm with elitism-control that favours the convergence, providing well distributed results along the efficient-fronts. A database of, approximately 1500 values, was generated, which used to check the numerical procedure. The representation of different properties is acceptably described with the multiproperty model constituted by the gE-model and its successive derivatives. In relation to other models, the approach carried out significantly improves the results because, in addition, it includes an estimation of the volumetric effects. A practical application was carried out with the simulation of a separation process for one of the systems that present a complex behaviour, providing solutions for its implementation in an industrial scale. | en_US |
dc.language | eng | en_US |
dc.relation | Mejoras en la producción de esteres en sistemas azeotrópicos para conseguir procesos sostenibles y eficientes. Ingeniería de procesos con métodos rigurosos, exper-model-simul | en_US |
dc.relation.ispartof | Journal of Industrial and Engineering Chemistry | en_US |
dc.source | Journal of Industrial and Engineering Chemistry[ISSN 1226-086X], v. 108, p. 288-307 | en_US |
dc.subject | 3303 ingeniería y tecnología químicas | en_US |
dc.subject | 330303 Procesos químicos | en_US |
dc.subject | 330311 Química industrial | en_US |
dc.subject.other | Experimentation | en_US |
dc.subject.other | Gibbs-Function | en_US |
dc.subject.other | Modelling | en_US |
dc.subject.other | Process Engineering | en_US |
dc.subject.other | Programming | en_US |
dc.subject.other | Simulation | en_US |
dc.title | The precision-complexity binomial to achieve the best mathematical-thermodynamic modelling on the Gibbs-function and its effect on the separation processes design | en_US |
dc.type | info:eu-repo/semantics/article | en_US |
dc.type | article | en_US |
dc.identifier.doi | 10.1016/j.jiec.2022.01.009 | en_US |
dc.identifier.scopus | 85124186589 | - |
dc.contributor.orcid | NO DATA | - |
dc.contributor.orcid | NO DATA | - |
dc.contributor.orcid | NO DATA | - |
dc.contributor.orcid | NO DATA | - |
dc.contributor.authorscopusid | 57188754800 | - |
dc.contributor.authorscopusid | 7402623992 | - |
dc.contributor.authorscopusid | 35112937200 | - |
dc.contributor.authorscopusid | 57216542630 | - |
dc.identifier.eissn | 2234-5957 | - |
dc.investigacion | Ingeniería y Arquitectura | en_US |
dc.type2 | Artículo | en_US |
dc.utils.revision | Sí | en_US |
dc.identifier.ulpgc | Sí | en_US |
dc.contributor.buulpgc | BU-ING | en_US |
dc.description.sjr | 1,005 | |
dc.description.jcr | 6,1 | |
dc.description.sjrq | Q1 | |
dc.description.jcrq | Q1 | |
dc.description.scie | SCIE | |
dc.description.miaricds | 10,9 | |
item.grantfulltext | none | - |
item.fulltext | Sin texto completo | - |
crisitem.project.principalinvestigator | Ortega Saavedra, Juan | - |
crisitem.author.dept | GIR IDeTIC: División de Ingeniería Térmica e Instrumentación | - |
crisitem.author.dept | IU para el Desarrollo Tecnológico y la Innovación | - |
crisitem.author.dept | Departamento de Enfermería | - |
crisitem.author.dept | GIR IDeTIC: División de Ingeniería Térmica e Instrumentación | - |
crisitem.author.dept | IU para el Desarrollo Tecnológico y la Innovación | - |
crisitem.author.dept | Departamento de Ingeniería de Procesos | - |
crisitem.author.dept | GIR IDeTIC: División de Ingeniería Térmica e Instrumentación | - |
crisitem.author.dept | IU para el Desarrollo Tecnológico y la Innovación | - |
crisitem.author.orcid | 0000-0001-5064-0565 | - |
crisitem.author.orcid | 0000-0002-6924-3444 | - |
crisitem.author.orcid | 0000-0003-1154-2633 | - |
crisitem.author.parentorg | IU para el Desarrollo Tecnológico y la Innovación | - |
crisitem.author.parentorg | IU para el Desarrollo Tecnológico y la Innovación | - |
crisitem.author.parentorg | IU para el Desarrollo Tecnológico y la Innovación | - |
crisitem.author.fullName | Sosa Marco,Adriel | - |
crisitem.author.fullName | Ortega García, Juan Miguel | - |
crisitem.author.fullName | Fernández Suárez, Luis Jesús | - |
crisitem.author.fullName | Lorenzo Pérez,Beatriz | - |
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