Please use this identifier to cite or link to this item: http://hdl.handle.net/2445/154357
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dc.contributor.authorExpósito, Sergi-
dc.contributor.authorBonet i Ruiz, Jordi-
dc.contributor.authorBonet Ruiz, Alexandra-
dc.contributor.authorLlorens Llacuna, Joan-
dc.contributor.authorIancu, Petrica-
dc.contributor.authorPlesu, Valentin-
dc.date.accessioned2020-03-30T06:39:12Z-
dc.date.available2020-03-30T06:39:12Z-
dc.date.issued2019-09-30-
dc.identifier.issn1974-9791-
dc.identifier.urihttp://hdl.handle.net/2445/154357-
dc.description.abstractMost of the distillation processes deal with multicomponent mixtures, existing a great quantity of distillation sequences for this process. The sharp splits available for an ideal ternary mixture are the direct and the inverse distillation sequence scheme in which the compounds are separated in two different columns. There are nonsharp splits in which all the compounds are separated in a single distillation column that can incorporate a side column. Unfortunately, to choose non-sharp splits schemes, there is no heuristic that can provide information about the recommended cases, e.g. a single distillation column in which the intermediate boiling compound is collected by a side stream at the required purity or by other possibilities, such as the use of a side stripper or a side rectifier. The literature about this subject is very scarce, and many times when the non-sharp splits are used, no comparison with the sharp split alternatives is provided. Therefore, the cases for which the literature suggests the use of side columns are further studied, e.g. BTX (Benzene, Toluene, Xylene) mixtures separation. For many case studies, the results obtained show that the energy savings achieved, due to the use of side columns, are not significantly higher than the best sharp split process schemes. However, these results do not discard that for some other situations; the side column could be the most advantageous case. Usually, it is considered that when the desired purity of the main product in a stream is reached, the impurities proportion do not affect significantly the energy consumption, and for most of the systems, this is true. However, for a mixture with a molar composition of 10 % isopentane, 10 % pentane and 80 % hexane (mol), when split in the respective compounds at a purity of 95 % (mol), very different energy requirements are depicted depending on the proportion of isopentane and hexane, present in the pentane stream obtained in a direct sequence process . The rigorous simulation results illustrate that almost 60% of the energy required to separate the abovementioned mixture is saved when the pentane stream carries a mixture of isopentane and hexane. In addition, the environmental impact has been analyzed for each case studied, being reduced in the same way as the energy consumption does-
dc.format.extent6 p.-
dc.format.mimetypeapplication/pdf-
dc.language.isoeng-
dc.publisherAIDIC-The Italian Association of Chemical Engineering-
dc.relation.isformatofReproducció del document publicat a: https://doi.org/10.3303/CET1976134-
dc.relation.ispartofChemical Engineering Transactions , 2019, vol. 76, p. 799-804-
dc.relation.urihttps://doi.org/10.3303/CET1976134-
dc.rights(c) AIDIC-The Italian Association of Chemical Engineering, 2019-
dc.subject.classificationDestil·lació-
dc.subject.otherDistillation-
dc.titleEnergy consumption in sharp and non-sharp splits of ideal ternary mixtures-
dc.typeinfo:eu-repo/semantics/article-
dc.typeinfo:eu-repo/semantics/publishedVersion-
dc.identifier.idgrec695824-
dc.date.updated2020-03-30T06:39:12Z-
dc.rights.accessRightsinfo:eu-repo/semantics/openAccess-
Appears in Collections:Articles publicats en revistes (Enginyeria Química i Química Analítica)

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