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An investigation of a model of the flow pattern transition mechanism in relation to the identification of annular flow of R134a in a vertical tube using various void fraction models and flow regime maps

dc.contributor.authorDalkilic, A. S.
dc.contributor.authorWongwises, S.
dc.contributor.institutionauthorDALKILIÇ, Ahmet Selim
dc.date.accessioned2026-06-27T12:51:44Z
dc.date.issued2010
dc.description.abstractIn the present study, new experimental data are presented for literature on the prediction of film thickness and identification of flow regime during the co-current downward condensation in a vertical smooth copper tube having an inner diameter of 8.1 mm and a length of 500 mm. R134a and water are used as working fluids in the tube side and annular side of a double tube heat exchanger, respectively. Condensation experiments are done at mass fluxes of 300 and 515 kg m(-2) s(-1). The condensing temperatures are between 40 and 50 degrees C: heat fluxes are between 12.65 and 66.61 kW m(-2). The average experimental heat transfer coefficient of the refrigerant HFC-134a is calculated by applying an energy balance based on the energy transferred from the test section. A mathematical model by Barnea et al. based on the momentum balance of liquid and vapor phases is used to determine the condensation film thickness of R134a. The comparative film thickness values are determined indirectly using relevant measured data together with various void fraction models and correlations reported in the open literature. The effects of heat flux, mass flux, and condensation temperature on the film thickness and condensation heat transfer coefficient are also discussed for the laminar and turbulent flow conditions. There is a good agreement between the film thickness results obtained from the theoretical model and those obtained from six of 35 void fraction models in the high mass flux region of R134a. In spite of their different valid conditions, six well-known flow regime maps from the literature are found to be predictive for the annular flow conditions in the test tube in spite of their different operating conditions. (C) 2010 Elsevier Inc. All rights reserved.en
dc.description.sponsorshipDepartment of Mechanical Engineering, King Mongkut's University of Technology Thonburi (KMUTT)
dc.description.sponsorshipThailand Research Fund
dc.description.sponsorshipKMUTT
dc.description.urihttps://doi.org/10.1016/j.expthermflusci.2009.12.011
dc.identifier.doi10.1016/j.expthermflusci.2009.12.011
dc.identifier.eissn1879-2286
dc.identifier.endpage705
dc.identifier.issn0894-1777
dc.identifier.issue6
dc.identifier.startpage692
dc.identifier.urihttps://hdl.handle.net/20.500.14981/47556
dc.identifier.volume34
dc.identifier.wos000278246100005
dc.language.isoeng
dc.publisherELSEVIER SCIENCE INC
dc.relation.ispartofEXPERIMENTAL THERMAL AND FLUID SCIENCE
dc.subjectCondensation
dc.subjectFlow regime map
dc.subjectVertical down flow
dc.subjectR134a
dc.subjectPhase change
dc.subjectHEAT-TRANSFER COEFFICIENT
dc.subject2-PHASE FRICTION FACTOR
dc.subjectHIGH-MASS FLUX
dc.subjectPRESSURE-DROP
dc.subjectDOWNWARD FLOW
dc.subjectHORIZONTAL TUBES
dc.subjectPART 1
dc.subjectDIAMETER
dc.subjectPREDICTION
dc.subjectThermodynamics
dc.subjectEngineering
dc.subjectPhysics
dc.titleAn investigation of a model of the flow pattern transition mechanism in relation to the identification of annular flow of R134a in a vertical tube using various void fraction models and flow regime maps
dc.typeArticle
dspace.entity.typePublication
local.import.sourceWOS

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