Modelling of multicomponent distillation for optimization and on-line control short-cut model and model adaptation

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creativework.keywordsModel adaptation, Multicomponent distillation, On-line control, Optimal mode of operation, Short-cut model
creativework.publisherUniversity of Chemical Technology and Metallurgyjournal@uctm.eduen
dc.contributor.authorKozarev N.
dc.date.accessioned2024-07-16T11:16:46Z
dc.date.accessioned2024-07-16T11:18:21Z
dc.date.available2024-07-16T11:16:46Z
dc.date.available2024-07-16T11:18:21Z
dc.date.issued2015-01-01
dc.description.abstractSome aspects of the multicomponent distillation modelling are analysed and discussed. A highly simplified noniterative mathematical model is offered for calculation of the top and bottom product compositions. It can be successfully adapted to a working distillation column on the base of easy obtainable measurement data related to the lower or upper cut points of the products. Being extremely fast, the model can be used for optimisation of the mode of operation and on-line control of crude oil separation and other multicomponent distillation processes.
dc.identifier.issn1314-7978
dc.identifier.issn1314-7471
dc.identifier.scopusSCOPUS_ID:84929087741en
dc.identifier.urihttps://rlib.uctm.edu/handle/123456789/1094
dc.language.isoen
dc.source.urihttps://www.scopus.com/inward/record.uri?partnerID=HzOxMe3b&scp=84929087741&origin=inward
dc.titleModelling of multicomponent distillation for optimization and on-line control short-cut model and model adaptation
dc.typeArticle
oaire.citation.issue3
oaire.citation.volume50
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