dc.contributor.author | Moukalled F. |
dc.contributor.author | Darwish M. |
dc.contributor.editor | |
dc.date | 2008 |
dc.date.accessioned | 2017-10-04T11:16:07Z |
dc.date.available | 2017-10-04T11:16:07Z |
dc.date.issued | 2008 |
dc.identifier | 10.1063/1.2912127 |
dc.identifier.isbn | |
dc.identifier.issn | 10706631 |
dc.identifier.uri | http://hdl.handle.net/10938/15069 |
dc.description.abstract | This paper deals with the formulation, implementation, and testing of three numerical techniques based on (i) a full multiphase approach, (ii) a multisize-group (MUSIG) approach, and (iii) a heterogeneous MUSIG (H-MUSIG) approach for the prediction of mixing and evaporation of liquid droplets injected into a stream of air. The numerical procedures are formulated following an Eulerian approach, within a pressure-based fully conservative finite volume method equally applicable in the subsonic, transonic, and supersonic regimes, for the discrete and continuous phases. The k-ε two-equation turbulence model is used to account for the droplet and gas turbulence with modifications to account for compressibility at high speeds. The performances of the various methods are compared by solving for two configurations involving streamwise and cross-stream sprayings into subsonic and supersonic streams. Results, which are displayed in the form of droplet velocity vectors, contour plots, and axial profiles, indicate that solutions obtained by the various techniques exhibit a similar behavior. Differences in values are relatively small with the largest being associated with droplet volume fractions and vapor mass fraction in the gas phase. This is attributed to the fact that with MUSIG and H-MUSIG, no droplet diameter equation is solved and the diameter of the various droplet phases is held constant, as opposed to the full multiphase approach. © 2008 American Institute of Physics. |
dc.format.extent | |
dc.language | English |
dc.publisher | MELVILLE |
dc.relation.ispartof | Publication Name: Physics of Fluids; Publication Year: 2008; Volume: 20; no. 4; |
dc.relation.ispartofseries | |
dc.relation.uri | |
dc.source | Scopus |
dc.subject.other | |
dc.title | Mixing and evaporation of liquid droplets injected into an air stream flowing at all speeds |
dc.type | Conference Paper |
dc.contributor.affiliation | Moukalled, F., Department of Mechanical Engineering, Faculty of Engineering and Architecture, American University of Beirut, Riad El-Solh 1107 2020 Beirut, Lebanon |
dc.contributor.affiliation | Darwish, M., Department of Mechanical Engineering, Faculty of Engineering and Architecture, American University of Beirut, Riad El-Solh 1107 2020 Beirut, Lebanon |
dc.contributor.authorAddress | Moukalled, F.; Department of Mechanical Engineering, Faculty of Engineering and Architecture, American University of Beirut, Riad El-Solh 1107 2020 Beirut, Lebanon |
dc.contributor.authorCorporate | University: American University of Beirut; Faculty: Faculty of Engineering and Architecture; Department: Mechanical Engineering; |
dc.contributor.authorDepartment | Mechanical Engineering |
dc.contributor.authorDivision | |
dc.contributor.authorEmail | |
dc.contributor.faculty | Faculty of Engineering and Architecture |
dc.contributor.authorInitials | Moukalled, F |
dc.contributor.authorInitials | Darwish, M |
dc.contributor.authorOrcidID | |
dc.contributor.authorReprintAddress | Moukalled, F (reprint author), Amer Univ Beirut, Fac Engn and Architecture, Dept Engn Mech, Riad El Solh 1107, Beirut 2020, Lebanon. |
dc.contributor.authorResearcherID | |
dc.contributor.authorUniversity | American University of Beirut |
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dc.description.citedCount | 2 |
dc.description.citedTotWOSCount | 2 |
dc.description.citedWOSCount | 2 |
dc.format.extentCount | 1 |
dc.identifier.articleNo | 40804 |
dc.identifier.coden | PHFLE |
dc.identifier.pubmedID | |
dc.identifier.scopusID | 43149092914 |
dc.identifier.url | |
dc.publisher.address | CIRCULATION and FULFILLMENT DIV, 2 HUNTINGTON QUADRANGLE, STE 1 N O 1, MELVILLE, NY 11747-4501 USA |
dc.relation.ispartofConference | |
dc.relation.ispartofConferenceCode | |
dc.relation.ispartofConferenceDate | |
dc.relation.ispartofConferenceHosting | |
dc.relation.ispartofConferenceLoc | |
dc.relation.ispartofConferenceSponsor | |
dc.relation.ispartofConferenceTitle | |
dc.relation.ispartofFundingAgency | |
dc.relation.ispartOfISOAbbr | Phys. Fluids |
dc.relation.ispartOfIssue | 4 |
dc.relation.ispartOfPart | |
dc.relation.ispartofPubTitle | Physics of Fluids |
dc.relation.ispartofPubTitleAbbr | Phys. Fluids |
dc.relation.ispartOfSpecialIssue | |
dc.relation.ispartOfSuppl | |
dc.relation.ispartOfVolume | 20 |
dc.source.ID | WOS:000255456600014 |
dc.type.publication | Journal |
dc.subject.otherAuthKeyword | |
dc.subject.otherChemCAS | |
dc.subject.otherIndex | Air streams |
dc.subject.otherIndex | Axial profiles |
dc.subject.otherIndex | Continuous phasis |
dc.subject.otherIndex | Contour plot |
dc.subject.otherIndex | Droplet diameters |
dc.subject.otherIndex | Droplet phasis |
dc.subject.otherIndex | Droplet velocity |
dc.subject.otherIndex | Eulerian approach |
dc.subject.otherIndex | Gas turbulence |
dc.subject.otherIndex | Gasphase |
dc.subject.otherIndex | Liquid droplets |
dc.subject.otherIndex | Multiphase approach |
dc.subject.otherIndex | Numerical procedures |
dc.subject.otherIndex | Numerical techniques |
dc.subject.otherIndex | Pressure-based |
dc.subject.otherIndex | Two-equation turbulence models |
dc.subject.otherIndex | Vapor mass |
dc.subject.otherIndex | Evaporation |
dc.subject.otherIndex | Finite volume method |
dc.subject.otherIndex | Liquids |
dc.subject.otherIndex | Mixing |
dc.subject.otherIndex | Multiphase flow |
dc.subject.otherIndex | Numerical methods |
dc.subject.otherIndex | Phase transitions |
dc.subject.otherIndex | Turbulence models |
dc.subject.otherIndex | Vapors |
dc.subject.otherIndex | Euler equations |
dc.subject.otherIndex | Flow velocity |
dc.subject.otherIndex | Subsonic flow |
dc.subject.otherIndex | Transonic flow |
dc.subject.otherIndex | Volume fraction |
dc.subject.otherIndex | Drops |
dc.subject.otherIndex | Full multiphase approach |
dc.subject.otherIndex | Mass fraction |
dc.subject.otherIndex | Multisize-group approach |
dc.subject.otherIndex | Drops |
dc.subject.otherIndex | Euler equations |
dc.subject.otherIndex | Evaporation |
dc.subject.otherIndex | Finite volume method |
dc.subject.otherIndex | Flow velocity |
dc.subject.otherIndex | Mixing |
dc.subject.otherIndex | Subsonic flow |
dc.subject.otherIndex | Transonic flow |
dc.subject.otherIndex | Turbulence models |
dc.subject.otherIndex | Volume fraction |
dc.subject.otherKeywordPlus | TURBULENT DISPERSIONS |
dc.subject.otherKeywordPlus | NUMERICAL-SIMULATION |
dc.subject.otherKeywordPlus | UNIFIED FORMULATION |
dc.subject.otherKeywordPlus | SPRAY EVAPORATION |
dc.subject.otherKeywordPlus | SEGREGATED CLASS |
dc.subject.otherKeywordPlus | MODELS |
dc.subject.otherKeywordPlus | COALESCENCE |
dc.subject.otherKeywordPlus | COMBUSTION |
dc.subject.otherKeywordPlus | COMPUTATION |
dc.subject.otherKeywordPlus | ALGORITHMS |
dc.subject.otherWOS | Mechanics |
dc.subject.otherWOS | Physics, Fluids and Plasmas |
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