homogeneous equilibrium
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Author(s):  
Sergei Frolov ◽  
Vladislav Ivanov ◽  
Nikolai Kuznetsov ◽  
Sergey Medvedev ◽  
Fedor Frolov ◽  
...  




2020 ◽  
Vol 13 (1) ◽  
pp. 129-168
Author(s):  
Joackim Bernier ◽  
◽  
Michel Mehrenberger ◽  


Shock Waves ◽  
2019 ◽  
Vol 29 (5) ◽  
pp. 769-793 ◽  
Author(s):  
F. Föll ◽  
T. Hitz ◽  
C. Müller ◽  
C.-D. Munz ◽  
M. Dumbser


2019 ◽  
Vol 27 (01) ◽  
pp. 1950001 ◽  
Author(s):  
Praveen Alok ◽  
Debjyoti Sahu

In this work, a set of computational investigation results of two-phase refrigerant flow through adiabatic capillary are presented. There are various sizes of capillary tubes that can be selected related to commercially available copper tubes. Earlier refrigerants and new refrigerants like R12, R22, R134a, R410A and R32 are used for the flow analysis. Homogeneous-equilibrium model is employed with user-defined properties of the refrigerants for computation using ANSYS CFX. Several important parameters can be predicted rapidly and accurately using this method such as refrigerant mass flow rate, vapor mass fraction, local Mach no. etc. The mean deviation in mass flow rate is found to be [Formula: see text]1.18% for the same length of capillary tube and the mean deviation of tube length is found to be [Formula: see text]1.48% for the same experimental mass flow rate with choked flow condition.



2019 ◽  
Vol 66 ◽  
pp. 1-21 ◽  
Author(s):  
Gloria Faccanoni ◽  
Hélène Mathis

This paper addresses the construction of admissible Equations of State (EoS) for compressible two-phase ows. We investigate two approaches. In the first one, the mixture is treated as a single uid with a complex thermodynamic. Most of the time the available EoS are determined experimentally and are often incomplete EoS, i.e. we know only the pressure as a function of the volume and the temperature. We present here a general framework to compute a complete EoS based on such an incomplete EoS. In the second approach, each phase is depicted by its own EoS. Following the Gibbs formalism, the mixture entropy is the sum of the phasic entropies which achieves its maximum at equilibrium. Depending on the miscibility of the mixture, one gets different geometrical properties on the resulting mixture entropy. Eventually we address the coupling of mixture EoS with the dynamic of the uid. Homogeneous Equilibrium and Relaxation Models (HEM and HRM) are introduced for an immiscible and a miscible two-phase mixture. Hyperbolicity is ensured taking advantage of the concavity properties of the mixture entropies.



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