Publication:
Droplet formation in a flow focusing configuration: effects of viscoelasticity

dc.contributor.coauthorN/A
dc.contributor.departmentN/A
dc.contributor.departmentN/A
dc.contributor.departmentDepartment of Mechanical Engineering
dc.contributor.departmentDepartment of Mechanical Engineering
dc.contributor.kuauthorNooranidoost, Mohammad
dc.contributor.kuauthorIzbassarov, Daulet
dc.contributor.kuauthorMuradoğlu, Metin
dc.contributor.kuprofilePhD Student
dc.contributor.kuprofilePhD Student
dc.contributor.kuprofileFaculty Member
dc.contributor.schoolcollegeinstituteGraduate School of Sciences and Engineering
dc.contributor.schoolcollegeinstituteGraduate School of Sciences and Engineering
dc.contributor.schoolcollegeinstituteCollege of Engineering
dc.contributor.yokidN/A
dc.contributor.yokidN/A
dc.contributor.yokid46561
dc.date.accessioned2024-11-09T23:29:03Z
dc.date.issued2016
dc.description.abstractWe numerically investigate the effects of bulk fluid viscoelasticity on droplet formation and dynamics in an axisymmetric flow focusing configuration. Viscoelasticity is modeled using the finitely extensible nonlinear elastic-Chilcott-Rallison (FENE-CR) model. Extensive simulations are performed to examine droplet formation and breakup dynamics for a wide range of parameters including flow rate ratio, Weissenberg number, polymeric viscosity ratio, and extensibility parameter. It is found that these parameters have a significant influence on the droplet size and size distribution (dispersity). Three different regimes are observed in the sequence of squeezing, dripping, and jetting modes as the flow rate ratio is increased. It is also found that the viscoelasticity has a similar effect as decreasing flow rate ratio and acts to delay transition from squeezing to dripping and from dripping to jetting regimes. the strain-rate hardening occurs at a critical Weissenberg number resulting in an abrupt increase in droplet size and this effect is more pronounced as the polymeric viscosity ratio is increased. Published by aIP Publishing.
dc.description.indexedbyWoS
dc.description.indexedbyScopus
dc.description.issue12
dc.description.openaccessNO
dc.description.publisherscopeInternational
dc.description.sponsoredbyTubitakEuTÜBİTAK
dc.description.sponsorshipScientific and Technical Research Council of Turkey (TUBITaK) [112M181] the authors are grateful to the Scientific and Technical Research Council of Turkey (TUBITaK) for the support of this research through Grant No. 112M181 and Turkish academy of Sciences (TUBa). the authors are grateful for the use of the computing facilities at TUBITaK-ULaKBIM, High Performance and Grid Computing Center.
dc.description.volume28
dc.identifier.doi10.1063/1.4971841
dc.identifier.eissn1089-7666
dc.identifier.issn1070-6631
dc.identifier.quartileQ1
dc.identifier.scopus2-s2.0-85006746667
dc.identifier.urihttp://dx.doi.org/10.1063/1.4971841
dc.identifier.urihttps://hdl.handle.net/20.500.14288/11981
dc.identifier.wos392092300005
dc.keywordsFront-tracking method
dc.keywordsDılute polymer-solutions
dc.keywords2-Phase flow
dc.keywordsBubbles
dc.keywordsComputations
dc.keywordsEmulsions
dc.keywordsMechanism
dc.keywordsBreakup
dc.keywordsFluids
dc.languageEnglish
dc.publisheramer inst Physics
dc.sourcePhysics of Fluids
dc.subjectMechanics
dc.subjectPhysics
dc.subjectFluids
dc.subjectPlasmas
dc.titleDroplet formation in a flow focusing configuration: effects of viscoelasticity
dc.typeJournal Article
dspace.entity.typePublication
local.contributor.authorid0000-0002-6326-9213
local.contributor.authorid0000-0003-4791-3803
local.contributor.authorid46561
local.contributor.kuauthorNooranidoost, Mohammad
local.contributor.kuauthorIzbassarov, Daulet
local.contributor.kuauthorMuradoğlu, Metin
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relation.isOrgUnitOfPublication.latestForDiscoveryba2836f3-206d-4724-918c-f598f0086a36

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