Приказ основних података о документу

dc.creatorJaćimović, Branislav M.
dc.creatorGenić, Srbislav
dc.creatorBudimir, Nikola
dc.creatorJarić, Marko
dc.date.accessioned2022-09-19T17:25:35Z
dc.date.available2022-09-19T17:25:35Z
dc.date.issued2014
dc.identifier.issn0017-9310
dc.identifier.urihttps://machinery.mas.bg.ac.rs/handle/123456789/1907
dc.description.abstractThis paper concerns techno-economic optimization of the production process of raw ethanol in a continuous distillation column as a part of the plant for production of rectified alcohol. Optimization was performed in order to determine the optimal ethanol concentration in the residue, which provides the minimum total production costs of existing plant. Total production costs are determined on the basis of experimental data, investment and operating costs and the estimated working life of the plant. It was found that ethanol concentration in the residue is significantly higher than values that can be found in the open literature.en
dc.publisherPergamon-Elsevier Science Ltd, Oxford
dc.relationMinistry of Education and Science of Serbia
dc.rightsrestrictedAccess
dc.sourceInternational Journal of Heat and Mass Transfer
dc.subjectRaw ethanolen
dc.subjectPlant optimizationen
dc.subjectCase studyen
dc.subjectBiofuelsen
dc.titleTechno-economic optimization of plant for raw ethanol production based on experimental dataen
dc.typearticle
dc.rights.licenseARR
dc.citation.epage646
dc.citation.other79: 639-646
dc.citation.rankaM21
dc.citation.spage639
dc.citation.volume79
dc.identifier.doi10.1016/j.ijheatmasstransfer.2014.07.085
dc.identifier.scopus2-s2.0-84907507016
dc.identifier.wos000343781900061
dc.type.versionpublishedVersion


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Приказ основних података о документу