The Navier-Stokes/Korteweg model (NSK) is a popular alternative model for simulating two-phase flows without introducing a phase-field \(\phi\). That model is a low Mach formulation of the Navier-Stokes equations, where \(\rho\) plays the role of phase index. The two-phase behavior is obtained by an appropriate choice of the Equation of State (EoS).
Several Equations of State (EoS) exist in the literature to simulate two-phase flows: Van der Waals, Carnahan-Starling, Peng-Robinson, Redlich-Kwong, etc. Only the first two have been tested in LBM_Saclay.
where \(T_k\) is a constant temperature which must be indicated in the input file as well as the two coefficients \(a,b\) and the constant of perfect gas \(R\). Such an equation of state is presented in Fig. 38 for five different temperatures (subscript \(k=1,...,5\)). That EoS can be derived from a thermodynamic potential (101) where \(\mathcal{W}_{vdW}\) is defined by
Finally the chemical potential \(\mu_{\rho}\) is derived by the Euler-Lagrange equation \(\mu_{\rho}=\mathcal{W}^{\prime}(\rho)-\kappa\boldsymbol{\nabla}^{2}\rho\):
On Fig. 37 the pressure is presented as a function of volume \(V\) whereas on Fig. 38 it is presented as a function of density \(\rho\). On those figures, one temperature \(T_5\) (the magenta curve) is above the critical temperature. The curve is monotonous and only one density corresponds to one pressure. For temperature \(T_4\) (cyan curve) there is an inflexion point corresponding to the critical temperature (zero derivative with respect to rho). At last, for three next temperatures \(T_1,T_2,T_3\) (respectively black, red and blue curves), the pressure presents a cubic form enabling the existence of two densities corresponding to one pressure.
In most of numerical methods that implement the NSK model, the pressure tensor Eq. (572) is not directly discretized because there exist two equivalent algebraic forms which are easier to implement. The first one is the potential form and the second involves the chemical potential.