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dc.creatorDukanović, Z.
dc.creatorDuričković, I.
dc.creatorGlišić, Sandra
dc.creatorOrlović, Aleksandar
dc.date.accessioned2021-03-10T11:13:20Z
dc.date.available2021-03-10T11:13:20Z
dc.date.issued2010
dc.identifier.isbn978-800202248-0
dc.identifier.urihttp://TechnoRep.tmf.bg.ac.rs/handle/123456789/1552
dc.description.abstractHydrotreating of middle distillates is one of the key processes in modern refining technology. Results of hydrotreating of gas oil and LCO blends, obtained in an industrial hydrotreater, are presented. Increasing temperature differences in the reactor with increasing content of LCO in the blend were observed along with substantial decrease of total sulfur in the product. A mathematical model of the industrial hydrotreater was developed to simulate the reactor behavior under different operating conditions. Cubic EOS were applied to model VLE of the reacting fluid for the ternary mixture composed of hydrogen, methane, and n-hexadecane. Validation of the model was performed using the available data obtained during the industrial test run. This is an abstract of a paper presented at the 7th European Congress of Chemical Engineering-7 and the 19th International Congress of Chemical and Process Engineering CHISA (Prague, Czech Republic 8/28/2010-9/1/2010).en
dc.publisher19th International Congress of Chemical and Process Engineering, CHISA 2010 and 7th European Congress of Chemical Engineering, ECCE-7
dc.rightsrestrictedAccess
dc.source19th International Congress of Chemical and Process Engineering, CHISA 2010 and 7th European Congres
dc.titleModelling of industrial trickle-bed reactor for hydrotreating of gas oil and light cycle oil blendsen
dc.typeconferenceObject
dc.rights.licenseARR
dc.identifier.pmid
dc.identifier.rcubhttps://hdl.handle.net/21.15107/rcub_technorep_1552
dc.identifier.scopus2-s2.0-84889922402
dc.type.versionpublishedVersion


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