CFD simulation of creeping flows in a novel split-and-recombine multifunctional reactor

dc.contributor.authoral-Hassan, Tamara
dc.contributor.authorHabchi, Charbel
dc.contributor.authorLemenand, Thierry
dc.contributor.authorAzizi, F.
dc.contributor.departmentDepartment of Chemical and Petroleum Engineering
dc.contributor.facultyMaroun Semaan Faculty of Engineering and Architecture (MSFEA)
dc.contributor.institutionAmerican University of Beirut
dc.date.accessioned2025-01-24T11:26:27Z
dc.date.available2025-01-24T11:26:27Z
dc.date.issued2021
dc.description.abstractVarious mixing processes deal with the blending of viscous fluids at low Reynolds numbers. Some of the emerging trends rely on the use of either active or passive microstructures to achieve this task when highly viscous or fragile fluids are employed. The compactness of such mixers remains, however, a major challenge due to the long residence times required to achieve the desired outcome. Split-and-Recombine (SAR) mixers are a promising solution since they rely on a multi-lamination process to perform a series of baker's transforms on the concentration profile. The current work is a numerical study that describes the hydrodynamic and mixing performance of a new topology of SAR mixers. This mixer is characterized by a double separation and recombination aimed at increasing the mixture homogeneity in a shorter distance. For this purpose, a finite element solver is used to compute the pressure drop, friction factor, concentration profile, and segregation scales for a viscous fluid in the creeping flow regime. The results are compared against two commonly used SAR mixers in the open literature. The findings show that the newly proposed mixer exhibits a superior performance through a better mixing quality at a lower energy consumption requirement. © 2021 Elsevier B.V.
dc.identifier.doihttps://doi.org/10.1016/j.cep.2021.108353
dc.identifier.eid2-s2.0-85101915494
dc.identifier.urihttp://hdl.handle.net/10938/26600
dc.language.isoen
dc.publisherElsevier B.V.
dc.relation.ispartofChemical Engineering and Processing - Process Intensification
dc.sourceScopus
dc.subjectCreeping flows
dc.subjectMicromixers
dc.subjectMixing efficiency
dc.subjectMultifunctional heat exchanger/reactor
dc.subjectPressure drop
dc.subjectScale of segregation
dc.subjectSplit-and-recombine
dc.subjectBlending
dc.subjectComputational fluid dynamics
dc.subjectEnergy utilization
dc.subjectReynolds number
dc.subjectViscosity
dc.subjectViscous flow
dc.subjectConcentration profiles
dc.subjectCreeping flow regime
dc.subjectFinite element solver
dc.subjectLong residence time
dc.subjectLow reynolds number
dc.subjectMixture homogeneity
dc.subjectMultifunctional reactor
dc.subjectMixers (machinery)
dc.titleCFD simulation of creeping flows in a novel split-and-recombine multifunctional reactor
dc.typeArticle

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