Volume 6: Fluids and Thermal Systems; Advances for Process Industries, Parts a and B 2011
DOI: 10.1115/imece2011-65539
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Prediction of Boiling and Critical Heat Flux Using an Eulerian Multiphase Boiling Model

Abstract: The present paper concerns the development and validation of an Eulerian multiphase boiling model to predict boiling and critical heat flux within the general-purpose computational fluid dynamics (CFD) solver FLUENT. The governing equations solved are generalized phase continuity, momentum and energy equations. Turbulence effects are accounted for using mixture, dispersed or per-phase multiphase turbulence models. Wall boiling phenomena are modeled using the baseline mechanistic nucleate boiling model, develop… Show more

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Cited by 32 publications
(32 citation statements)
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“…_ m rq denotes the mass transfer from r th to q th phase, while _ m qr is the mass transfer from q th to r th phase. s q is the external mass source applied on the q th phase (Li et al, 2011).…”
Section: Governing Equationsmentioning
confidence: 99%
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“…_ m rq denotes the mass transfer from r th to q th phase, while _ m qr is the mass transfer from q th to r th phase. s q is the external mass source applied on the q th phase (Li et al, 2011).…”
Section: Governing Equationsmentioning
confidence: 99%
“…In equation (2), p is pressure, t ¼ q is stress-strain tensor in the q th phase, B f is the body force, F D rq is the interaction drag force between the two phases, F TD rq is the turbulent dispersed force, V rq and V qr are relative velocity vectors between the two phases, and F q , F L q and F vm q are the external body, lift and virtual mass exchange forces, respectively (Li et al, 2011).…”
Section: Governing Equationsmentioning
confidence: 99%
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“…The development of a full 3D mechanistic model of the flow boiling process is challenging [26] due to the complex nature of the processes involved (activation of nucleation sites, bubble dynamics, and interfacial heat transfers) and the computational needs required for the solution of the direct numerical problem, which incorporates a large number of bubbles and surfaces with complex geometries [27,28]. To overcome this challenge, semi-mechanistic approaches are proposed [29][30][31][32][33][34]. For example, Kurul and Podowski developed a 3D model which couples an Euler-Euler two-phase flow model (for bulk fluid flow) with a wall boiling model.…”
Section: Introductionmentioning
confidence: 99%