Please use this identifier to cite or link to this item: http://hdl.handle.net/11452/33001
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dc.contributor.authorSakin, Ali-
dc.date.accessioned2023-06-09T12:24:31Z-
dc.date.available2023-06-09T12:24:31Z-
dc.date.issued2019-10-
dc.identifier.citationSakin, A. vd. (2019). ''Performance analysis of axial and reverse flow cyclone separators''. Chemical Engineering and Processing-Process Intensification, 144.en_US
dc.identifier.issn0255-2701-
dc.identifier.issn1873-3204-
dc.identifier.urihttps://doi.org/10.1016/j.cep.2019.107630-
dc.identifier.urihttps://www.sciencedirect.com/science/article/pii/S0255270118313709-
dc.identifier.urihttp://hdl.handle.net/11452/33001-
dc.description.abstractPerformance characteristics of a novel cyclone with tangential inlet were presented in axial and reverse flow operation modes. 3-D and unsteady governing equations were used for the numerical solution of the two-phase turbulent flow in the cyclone separator. The Eulerian approach was used to solve the flow field, and the Reynolds Stress Model (RSM) with the scalable wall function was employed for the numerical study. The Lagrangian approach with the Discrete Phase Model was used to calculate the discrete phase by releasing particles from the inlet surface. CFD calculations were run for different geometric configurations to analyze the performance of the cyclones regarding pressure drop, cut-off diameter, and fractional efficiency. Axial and tangential velocity profiles are presented at the defined sections. The computational results of pressure drop, velocity field, and separation efficiency were also compared for the axial and reverse flow cyclones at the same flow rate. The results show that pressure drop and collection efficiency in reverse flow mode are higher than that of the axial flow operation. However, axial flow cyclones seem to be more efficient for small particles comparing to reverse flow cyclones.en_US
dc.language.isoenen_US
dc.publisherElsevieren_US
dc.rightsinfo:eu-repo/semantics/openAccessen_US
dc.subjectTwo phase flowen_US
dc.subjectSeparation efficiencyen_US
dc.subjectPressure dropen_US
dc.subjectCfden_US
dc.subjectDimensionsen_US
dc.subjectFielden_US
dc.subjectEnergy & Fuelsen_US
dc.subjectEngineeringen_US
dc.subjectAxial flowen_US
dc.subjectComputational fluid dynamicsen_US
dc.subjectCyclone separatorsen_US
dc.subjectDropsen_US
dc.subjectEfficiencyen_US
dc.subjectLagrange multipliersen_US
dc.subjectPressure dropen_US
dc.subjectReynolds numberen_US
dc.subjectVelocityen_US
dc.subjectWall functionen_US
dc.subjectComputational resultsen_US
dc.subjectFractional efficienciesen_US
dc.subjectGeometric configurationsen_US
dc.subjectLa-grangian approachesen_US
dc.subjectPerformance characteristicsen_US
dc.subjectReverse-flow operationen_US
dc.subjectReynolds stress modelsen_US
dc.subjectSeparation efficiencyen_US
dc.subjectTwo phase flowen_US
dc.titlePerformance analysis of axial and reverse flow cyclone separatorsen_US
dc.typeArticleen_US
dc.identifier.wos000500038100007tr_TR
dc.identifier.scopus2-s2.0-85071402548tr_TR
dc.relation.tubitakTÜBİTAK 114M591tr_TR
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergitr_TR
dc.contributor.departmentBursa Uludağ Üniversitesi/Mühendislik Fakültesi/Makina Mühendisliği/Termodinamik Bölümü.tr_TR
dc.contributor.orcid0000-0002-7442-2746tr_TR
dc.identifier.volume144tr_TR
dc.relation.journalChemical Engineering and Processing-Process Intensificationen_US
dc.contributor.buuauthorKaragöz, Irfan-
dc.contributor.buuauthorAvcı, Atakan-
dc.contributor.researcheridAAB-9388-2020tr_TR
dc.relation.collaborationYurt içitr_TR
dc.subject.wosEnergy & fuelsen_US
dc.subject.wosEngineering, chemicalen_US
dc.indexed.wosSCIEen_US
dc.indexed.scopusScopusen_US
dc.wos.quartileQ2en_US
dc.contributor.scopusid56785809700tr_TR
dc.contributor.scopusid7004169972tr_TR
dc.subject.scopusCyclone Separators; Gas; Pressure Dropen_US
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