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A simple and fast phase transition relaxation solver for compressible multicomponent two-phase flows

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Academic year: 2021

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Table 1: Noble Abel Stiffened Gas (NASG) coefficients for water and air determined in the temperature range [273 − 500 K]
Figure 1: Comparison between experimental and theoretical saturation curves for liquid water and steam with coefficients determined in the temperature range [273 − 500 K]
Figure 2: Equilibrium mass fractions obtained from water liquid/vapor, as a function of the air mass fraction.
Figure 3: Illustration of the algorithm for the multicomponent phase transition solver
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