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dc.creatorMijatović, Ivana M.
dc.creatorGlišić, Sandra
dc.creatorOrlović, Aleksandar
dc.date.accessioned2021-03-10T12:27:58Z
dc.date.available2021-03-10T12:27:58Z
dc.date.issued2014
dc.identifier.issn0888-5885
dc.identifier.urihttp://TechnoRep.tmf.bg.ac.rs/handle/123456789/2722
dc.description.abstractReducing the sulfur content of diesel fuels may require adjusted operation of low-pressure hydrotreater units. A mathematical model for co-hydrotreating of straight run gas oil blended with fluid catalytic cracking naphtha and light cycle oil was developed using an axial distribution of phase equilibrium and effective wetting in the catalytic reactor. The model assumes that hydrodesulfurization (HDS) and hydrodearomatization reactions occur on the catalyst surface which is in contact with the vapor or liquid phase. Kinetic equations of HougenWatson type were used to describe HDS reactions for different classes of sulfur compounds. Model results were validated using the industrial test run data, and very good predictions of overall sulfur conversion and reactor temperature were obtained. Simulations of reactor operation at different pressures, temperatures, and H-2 purities confirm that reaction pressures of around 100 bar and high-purity hydrogen streams are required for almost complete removal of sulfur compounds.en
dc.publisherAmer Chemical Soc, Washington
dc.relationinfo:eu-repo/grantAgreement/MESTD/Integrated and Interdisciplinary Research (IIR or III)/45019/RS//
dc.relationinfo:eu-repo/grantAgreement/EC/FP7/245916/EU//
dc.rightsrestrictedAccess
dc.sourceIndustrial & Engineering Chemistry Research
dc.titleModeling a Catalytic Reactor for Hydrotreating of Straight-Run Gas Oil Blended with Fluid Catalytic Cracking Naphtha and Light Cycle Oil: Influence of Vapor-Liquid Equilibriumen
dc.typearticle
dc.rights.licenseARR
dc.citation.epage19116
dc.citation.issue49
dc.citation.other53(49): 19104-19116
dc.citation.rankM21
dc.citation.spage19104
dc.citation.volume53
dc.identifier.doi10.1021/ie503188p
dc.identifier.scopus2-s2.0-84949115743
dc.identifier.wos000346322200054
dc.type.versionpublishedVersion


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