2009
DOI: 10.1016/j.compfluid.2009.03.001
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Numerical simulation of cavitating flows with homogeneous models

Abstract: The simulation of cavitating flows is a challenging problem both in terms of modelling the physics and developing robust numerical methodologies. Such flows are characterized by important variations of the local Mach number and involve thermodynamic phase transition. To simulate these flows by applying homogeneous models, an appropriate equation of state (EOS) is necessary to cover all possible fluid states (pure liquid, two-phase mixture and pure vapour). Moreover, the numerical method has to handle any Mach … Show more

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Cited by 168 publications
(111 citation statements)
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“…It is composed of three conservation laws for mixture quantities completed by an equation for a non-conservative quantity describing the flow topology, usually the void ratio [21,11]. With the assumption of complete thermodynamic equilibrium between phases (local temperature, pressure, and free Gibbs enthalpy equality between phases), the three-equation models or Homogeneous Equilibrium Models (HEM) are derived [12,34].…”
Section: Introductionmentioning
confidence: 99%
“…It is composed of three conservation laws for mixture quantities completed by an equation for a non-conservative quantity describing the flow topology, usually the void ratio [21,11]. With the assumption of complete thermodynamic equilibrium between phases (local temperature, pressure, and free Gibbs enthalpy equality between phases), the three-equation models or Homogeneous Equilibrium Models (HEM) are derived [12,34].…”
Section: Introductionmentioning
confidence: 99%
“…The speed of sound within the mixture can be represented as a function of the enthalpy of each phase (Goncalves & Patella 2009):…”
Section: A Mixture Of Stiffened Gas Eosmentioning
confidence: 99%
“…The drift flux accounts for the thermodynamic nonequilibrium (metastable conditions can be described) by solving the transport equation of the vapor mass fraction Y (Fig. 3), whereas the homogeneous model is purely empirical and estimates the vapor mass fraction from mixture properties (energy, 19 density, 20 etc.). In the first approach, the vapor mass fraction transport equation reads…”
Section: Standard Approach: the Eulerian Formulationmentioning
confidence: 99%