Please use this identifier to cite or link to this item: http://hdl.handle.net/10397/104151
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dc.contributorDepartment of Industrial and Systems Engineering-
dc.creatorSun, Sen_US
dc.creatorChun, Wen_US
dc.creatorYang, Aen_US
dc.creatorShen, Wen_US
dc.creatorCui, Pen_US
dc.creatorRen, Jen_US
dc.date.accessioned2024-02-05T08:46:43Z-
dc.date.available2024-02-05T08:46:43Z-
dc.identifier.issn0360-5442en_US
dc.identifier.urihttp://hdl.handle.net/10397/104151-
dc.language.isoenen_US
dc.publisherElsevier Ltden_US
dc.rights© 2020 Elsevier Ltd. All rights reserved.en_US
dc.rights© 2020. This manuscript version is made available under the CC-BY-NC-ND 4.0 license https://creativecommons.org/licenses/by-nc-nd/4.0/en_US
dc.rightsThe following publication Sun, S., Chun, W., Yang, A., Shen, W., Cui, P., & Ren, J. (2020). The separation of ternary azeotropic mixture: Thermodynamic insight and improved multi-objective optimization. Energy, 206, 118117 is available at https://doi.org/10.1016/j.energy.2020.118117.en_US
dc.subjectConceptual designen_US
dc.subjectMulti-objective optimizationen_US
dc.subjectTernary azeotropic mixtureen_US
dc.subjectTriple-column extractive distillationen_US
dc.titleThe separation of ternary azeotropic mixture : thermodynamic insight and improved multi-objective optimizationen_US
dc.typeJournal/Magazine Articleen_US
dc.identifier.volume206en_US
dc.identifier.doi10.1016/j.energy.2020.118117en_US
dcterms.abstractAcetonitrile (ACN) and Ethanol (EtOH) are important organic solvents and they are frequently used as mobile phase in high performance liquid chromatography resulting in the production of waste ternary mixture ACN/EtOH/water. The separation of such ternary systems is a key to recovery valuable solvents in waste liquid from views on economic and environmental benefits. Thus, we proposed an effective separation strategy of triple-column extractive distillation (TCED) to separate such ternary mixture with three binary azeotropes and a single ternary azeotrope for the first time. The suitable entrainer and the separation sequence were determined by thermodynamic insights (i.e., residue curve maps, isovolatility line, univolatility line and material balance lines). In addition, an improved multi-objective genetic algorithm optimization embedding the weak mutation and detection/deduplication of overlapping solutions was employed to optimize the proposed process with plenty of continuous and discrete decision variables. Finally, DMSO was determined as the most appropriate entrainer to separate such complex ternary mixture. The separation sequence of TCED process was determined as the ACN first, then EtOH and water as the last product. The optimal TCED process with the trade-off benefits between fixed capital investment and annual operating costs was obtained.-
dcterms.accessRightsopen accessen_US
dcterms.bibliographicCitationEnergy, 1 Sept 2020, v. 206, 118117en_US
dcterms.isPartOfEnergyen_US
dcterms.issued2020-09-01-
dc.identifier.scopus2-s2.0-85087088271-
dc.identifier.eissn1873-6785en_US
dc.identifier.artn118117en_US
dc.description.validate202402 bcch-
dc.description.oaAccepted Manuscripten_US
dc.identifier.FolderNumberISE-0261-
dc.description.fundingSourceOthersen_US
dc.description.fundingTextThe National Natural Science Foundation of China; the Fundamental Research Funds for the Central Universitiesen_US
dc.description.pubStatusPublisheden_US
dc.identifier.OPUS23574427-
dc.description.oaCategoryGreen (AAM)en_US
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