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Please use this identifier to cite or link to this item: http://10.10.120.238:8080/xmlui/handle/123456789/938
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dc.contributor.authorYadav A.en_US
dc.contributor.authorRoy S.en_US
dc.date.accessioned2023-11-30T08:56:49Z-
dc.date.available2023-11-30T08:56:49Z-
dc.date.issued2022-
dc.identifier.issn0008-4034-
dc.identifier.otherEID(2-s2.0-85114094420)-
dc.identifier.urihttps://dx.doi.org/10.1002/cjce.24280-
dc.identifier.urihttp://localhost:8080/xmlui/handle/123456789/938-
dc.description.abstractA mixing cell network (MCN) was developed for the commercial diesel hydrodesulphurization process (DHDS) in a trickle bed reactor (TBR). The two-phase model is developed to simulate the performance of an industrial DHDS unit. Major hydrotreating reactions such as hydrodesulphurization (HDS), hydrodearomatization (HDA), and olefin saturation were accounted for in the developed model. The MCN model predictions on axial concentration profiles of sulphur, polynuclear aromatics (PNAs), monoaromatics (MAs), and temperature were found to be in agreement with the real-time plant data. Further, the predicted results were also compared with the plug flow model to confirm model adequacy. The results obtained in this paper show the efficacy of the MCN model in simulating multiple reactions happening in real industrial scenarios. © 2021 Canadian Society for Chemical Engineering.en_US
dc.language.isoenen_US
dc.publisherJohn Wiley and Sons Incen_US
dc.sourceCanadian Journal of Chemical Engineeringen_US
dc.subjecthydroprocessingen_US
dc.subjecthydrotreatingen_US
dc.subjectkinetic modelen_US
dc.subjectmixing cell networken_US
dc.subjecttrickle bed reactoren_US
dc.titleModelling of hydrodesulphurization in industrial trickle bed reactor using mixing cell network approachen_US
dc.typeJournal Articleen_US
Appears in Collections:Journal Article

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