Two-Phase Thermodynamic Equilibrium

The Two-Phase Thermodynamic Equilibrium is a multiphase mixture approach that is restricted to modeling two phases. With this model Simcenter STAR-CCM+ solves the mass, momentum, and energy as mixture quantities rather than phase quantities. Therefore, the computational efforts are reduced by assuming the suspension to be a homogeneous single-phase system.

The Two-Phase Thermodynamic Equilibrium model is designed to model applications that involve two phases of the same substance, typically water and steam. The distribution of static enthalpy and the assumption of thermodynamic equilibrium are used to calculate the distribution of phases.

Examples of industrial applications of the Two-Phase Thermodynamic Equilibrium model include steam generators, boilers, and steam turbines.

This model covers three different levels of approximation:
  • Zero Slip model (default)
    The multiphase mixture is treated as a homogeneous single-phase system, with the following assumptions ([634], [640]):
    • The mixture of phases behaves as a single fluid.

      A single set of transport equations for mass, momentum, and energy is solved for the mixture as a whole. You set the properties of the individual phases, and specify the phase volume fractions. The density, viscosity, and other fluid properties are calculated from the phase properties and phase volume fractions, based on the assumption of homogeneity.

    • The phases are in thermal equilibrium.

      The two phases have the same temperature and the phase distribution is computed based on heat balance.

    • There is no relative/slip velocity between the phases.

    • The phases flow through a porous medium with porosity χ .

  • Algebraic Slip model

    This model uses empirical correlations for the slip ratio between phase velocities to calculate the void fraction. However, the kinematic effect of relative motion between the phases is not accounted for.

    This approach provides a better estimate of the distribution of void fraction and mixture density than the homogenous model.

  • Drift Flux model.

    This model accounts for the kinematic effects of relative motion between the phases.

    The relative motion is defined using kinematic constitutive equations for the particular flow regime and thermal-hydraulic conditions.

The only supported phase interaction with Two-Phase Thermodynamic Equilibrium model is Boiling.