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dc.contributor.authorÇırpıcı, Burak Kaan
dc.contributor.authorRogers, B. D.
dc.contributor.authorWang, Y. C.
dc.date.accessioned2022-05-11T14:26:38Z
dc.date.available2022-05-11T14:26:38Z
dc.date.issued2016
dc.identifier.urihttps://hdl.handle.net/20.500.11776/6525
dc.description9th International Conference on Computational Fluid Dynamics, ICCFD 2016 -- 11 July 2016 through 15 July 2016 -- -- 159582en_US
dc.description.abstractModelling of the expansion of 3-D single bubble using a multi-phase model has been developed for GIVE APPLICATION AREA with the potential of a meshless numerical simulation method, Smoothed Particle Hydrodynamics (SPH), and the consideration of the surface tension between phases and viscosity effect of the polymer melt surrounding the bubble. Mainly, bubble growth in the polymer material occurs because of the mass conversion (mass loss) from the polymer melt to gas due to heat such as fire. This mass conversion drives the expansion process of the gas bubble by increasing the pressure inside. To represent the mass transfer the from the polymer melt to the bubble, this paper proposes a novel algorithm to increase number of SPH gas particles inside the bubble during the simulation. The present paper aims to explain this new developed method including particle shifting scheme identifying the main challenges of dynamic and non-spherical bubble modelling which have a nonlinear multi-phase behaviour. In order to develop stable simulations for the multi-phase bubble growth in isothermal conditions in millimeter scale, surface tension effects have been scaled according to the Capillary number. The insertion of the new gas particles into the bubble centre has been performed at regular intervals to identify the influence of time period of particle insertion. The predicted results from the numerical study have been compared with the well-known analytical solution for single bubble growth for final bubble radius and bubble growth rate. Time step analysis has also been performed to show the numerical stability for this kind of bubble growth simulation. The importance of the particle shifting scheme has also been addressed for simulating bubble growth in this multi-phase problem. © 2016 9th International Conference on Computational Fluid Dynamics, ICCFD 2016 - Proceedings. All rights reserved.en_US
dc.language.isoengen_US
dc.publisherInternational Conference on Computational Fluid Dynamics 2016en_US
dc.rightsinfo:eu-repo/semantics/closedAccessen_US
dc.subjectBubble growthen_US
dc.subjectMulti-phaseen_US
dc.subjectSmoothed Particle Hydrodynamics (SPH)en_US
dc.subjectSurface tensionen_US
dc.subjectViscosityen_US
dc.subjectBubbles (in fluids)en_US
dc.subjectComputational fluid dynamicsen_US
dc.subjectGasesen_US
dc.subjectGrowth rateen_US
dc.subjectHigh pressure effectsen_US
dc.subjectMass transferen_US
dc.subjectNumerical methodsen_US
dc.subjectPolymer meltsen_US
dc.subjectSurface tensionen_US
dc.subjectThree dimensional computer graphicsen_US
dc.subjectCapillary numbersen_US
dc.subjectIsothermal conditionsen_US
dc.subjectNumerical simulation methoden_US
dc.subjectPolymer materialsen_US
dc.subjectSingle gas bubblesen_US
dc.subjectSmoothed particle hydrodynamicsen_US
dc.subjectSurface tension effectsen_US
dc.subjectViscosity effectsen_US
dc.subjectHydrodynamicsen_US
dc.titleSimulating 3-D single gas bubble growth in a polymer melt using multi-phase SPHen_US
dc.typeconferencePaperen_US
dc.relation.ispartof9th International Conference on Computational Fluid Dynamics, ICCFD 2016 - Proceedingsen_US
dc.departmentFakülteler, Çorlu Mühendislik Fakültesi, İnşaat Mühendisliği Bölümüen_US
dc.institutionauthorÇırpıcı, Burak Kaan
dc.relation.publicationcategoryKonferans Öğesi - Uluslararası - Kurum Öğretim Elemanıen_US
dc.authorscopusid57113661500
dc.authorscopusid57208381722
dc.authorscopusid57215292641
dc.identifier.scopus2-s2.0-85086287506en_US


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