Abstract:The aim of this work is to improve the accuracy of cavitating flow simulations by considering realfuel mixture thermodynamics, like gas (air) solubility and physical property deviations from ideality, and their effects on phase change. In this work, a new fully compressible two-phase six-equations model coupled with Peng and Robinson [1] real-fluid cubic equation of state (PR-EOS) is described. Assuming thermodynamic equilibrium with negligible capillarity, this diffuse interface model has been implemented in … Show more
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