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dc.creatorStamenić, Marko
dc.creatorDikić, Vladimir
dc.creatorMandić, Miloš
dc.creatorTodić, Branislav
dc.creatorBukur, Dragomir B.
dc.creatorNikačević, Nikola
dc.date.accessioned2021-03-10T13:21:00Z
dc.date.available2021-03-10T13:21:00Z
dc.date.issued2017
dc.identifier.issn0888-5885
dc.identifier.urihttp://TechnoRep.tmf.bg.ac.rs/handle/123456789/3542
dc.description.abstractA multiphase fixed-bed reactor (FBR) model for Fischer Tropsch Synthesis has been developed. A high level of details is considered for description of the phenomena on the reactor and particle scale. Detailed kinetics is used, with parameters estimated from experiments with a cobalt-based catalyst. Model robustness has been validated using literature data. Performance analysis was made for a conventional scale FBR with egg-shell distribution of catalyst and a millimeter-scale FBR with small particles and uniform distribution. In both cases, diffusion limitations are almost eliminated due to use of small diffusion lengths. For similar qualitative results, a milli-scaled design would result in a significantly lower reactor volume, but the capital costs could be high due to large wall area and a vast number of tubes. Heat removal is efficient in both cases, and pressure drop in the milli-scale reactor is low due to the use of a shorter bed and lower velocity.en
dc.publisherAmer Chemical Soc, Washington
dc.relationQatar National Research Fund (a member of the Qatar Foundation) [NPRP 7-559-2-211]
dc.rightsrestrictedAccess
dc.sourceIndustrial & Engineering Chemistry Research
dc.titleMultiscale and Multiphase Model of Fixed Bed Reactors for Fischer-Tropsch Synthesis: Intensification Possibilities Studyen
dc.typearticle
dc.rights.licenseARR
dc.citation.epage9979
dc.citation.issue36
dc.citation.other56(36): 9964-9979
dc.citation.rankM21
dc.citation.spage9964
dc.citation.volume56
dc.identifier.doi10.1021/acs.iecr.7b02467
dc.identifier.rcubconv_5399
dc.identifier.scopus2-s2.0-85029354528
dc.identifier.wos000411043700005
dc.type.versionpublishedVersion


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