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Journal articles on the topic 'Compressible Two-Phase Flow'

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Published: 4 June 2021
Last updated: 25 May 2024

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1

Jin, H., J. Glimm, and D. H. Sharp. "Compressible two-pressure two-phase flow models." Physics Letters A 353, no. 6 (May 2006): 469–74. http://dx.doi.org/10.1016/j.physleta.2005.11.087.

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2

Jin, Hyeonseong, and James Glimm. "Weakly compressible two-pressure two-phase flow." Acta Mathematica Scientia 29, no. 6 (November 2009): 1497–540. http://dx.doi.org/10.1016/s0252-9602(10)60001-x.

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3

Lung-an, Ying. "Two phase compressible flow in porous media." Acta Mathematica Scientia 31, no. 6 (November 2011): 2159–68. http://dx.doi.org/10.1016/s0252-9602(11)60391-3.

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4

Aboulhasanzadeh, Bahman, and Kamran Mohseni. "An observable regularization of compressible two-phase flow." Procedia Computer Science 108 (2017): 1943–52. http://dx.doi.org/10.1016/j.procs.2017.05.176.

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5

Trimulyono, Andi, S. Samuel, and Muhammad Iqbal. "Sloshing Simulation of Single-Phase and Two-Phase SPH using DualSPHysics." Kapal: Jurnal Ilmu Pengetahuan dan Teknologi Kelautan 17, no. 2 (June 4, 2020): 50–57. http://dx.doi.org/10.14710/kapal.v17i2.27892.

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The sloshing phenomenon is one of the free surface flow that can endanger liquid cargo carriers such as ships. Sloshing is defined as the resonance of fluid inside a tank caused by external oscillation. When sloshing is close to the natural frequency of the tank it could endanger ships. Particle method has the advantages to be applied because sloshing is dealing with free surface. One of the particle methods is Smoothed Particle Hydrodynamics (SPH). In this study, compressible SPH was used as a result of the pressure oscillation, which exists because of the effect of density fluctuation as nature of weakly compressible SPH. To reduce pressure noise, a filtering method, Low Pass Filter, was used to overcome pressure oscillation. Three pressure sensors were used in the sloshing experiment with a combination of motions and filling ratios. Only one pressure sensor located in the bottom was used to validate the numerical results. A set of SPH parameters were derived that fit for the sloshing problem. The SPH results show a good agreement with the experiment’s. The difference between SPH and experiment is under 1 % for sway, but a larger difference shows in roll. Low pass filter technique could reduce pressure noise, but comprehensive method needs to develop for general implementation.
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6

Hewedy, N. I. I., M. H. Hamed, A. F. M. Mahrous, and T. A. Ghonim. "Performance Prediction of Compressible Two-Phase Flow through Ejectors." ERJ. Engineering Research Journal 38, no. 1 (January 1, 2015): 31–46. http://dx.doi.org/10.21608/erjm.2015.66773.

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7

WOHLETZ, K. "Chapter 7 Pyroclastic surges and compressible two-phase flow." Developments in Volcanology 4 (1998): 247–312. http://dx.doi.org/10.1016/s1871-644x(01)80008-5.

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8

BURMAN, E. "ADAPTIVE FINITE ELEMENT METHODS FOR COMPRESSIBLE TWO-PHASE FLOW." Mathematical Models and Methods in Applied Sciences 10, no. 07 (October 2000): 963–89. http://dx.doi.org/10.1142/s0218202500000495.

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We apply the adaptive streamline diffusion method for compressible flow in conservation variables using P1×P0 finite elements to a conservative model of two-phase flow. The adaptive algorithm is based on an a posteriori error estimate involving certain stability factors related to a linearized dual problem. For a model problem we prove that the stability factors are bounded. We compute the stability factors for some numerical examples in one- and two-space dimensions.
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9

Amaziane, B., and L. Pankratov. "Homogenization of compressible two-phase two-component flow in porous media." Nonlinear Analysis: Real World Applications 30 (August 2016): 213–35. http://dx.doi.org/10.1016/j.nonrwa.2016.01.006.

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10

Jin, H., J. Glimm, and D. H. Sharp. "Entropy of averaging for compressible two-pressure two-phase flow models." Physics Letters A 360, no. 1 (December 2006): 114–21. http://dx.doi.org/10.1016/j.physleta.2006.07.064.

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11

El Ouafa, Simon, Stephane Vincent, Vincent Le Chenadec, Benoît Trouette, Syphax Ferreka, and Amine Chadil. "A Compressible Formulation of the One-Fluid Model for Two-Phase Flows." Fluids 9, no. 4 (April 12, 2024): 90. http://dx.doi.org/10.3390/fluids9040090.

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In this paper, we introduce a compressible formulation for dealing with 2D/3D compressible interfacial flows. It integrates a monolithic solver to achieve robust velocity–pressure coupling, ensuring precision and stability across diverse fluid flow conditions, including incompressible and compressible single-phase and two-phase flows. Validation of the model is conducted through various test scenarios, including Sod’s shock tube problem, isothermal viscous two-phase flows without capillary effects, and the impact of drops on viscous liquid films. The results highlight the ability of the scheme to handle compressible flow situations with capillary effects, which are important in computational fluid dynamics (CFD).
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12

Tunkeaw, Jiratrakul, and Watchapon Rojanaratanangkule. "A Discontinuity-Capturing Methodology for Two-Phase Inviscid Compressible Flow." Engineering Journal 25, no. 11 (November 30, 2021): 45–56. http://dx.doi.org/10.4186/ej.2021.25.11.45.

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13

Ahmed, Munshoor, M. Rehan Saleem, Saqib Zia, and Shamsul Qamar. "Central Upwind Scheme for a Compressible Two-Phase Flow Model." PLOS ONE 10, no. 6 (June 3, 2015): e0126273. http://dx.doi.org/10.1371/journal.pone.0126273.

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14

Saad, Mazen. "Slightly compressible and immiscible two-phase flow in porous media." Nonlinear Analysis: Real World Applications 15 (January 2014): 12–26. http://dx.doi.org/10.1016/j.nonrwa.2013.04.008.

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15

Chen, Yupin, Yuefan Deng, James Glimm, Gang Li, Qiang Zhang, and David H. Sharp. "A renormalization group scaling analysis for compressible two‐phase flow." Physics of Fluids A: Fluid Dynamics 5, no. 11 (November 1993): 2929–37. http://dx.doi.org/10.1063/1.858701.

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16

Zhang, Lingxin, and Boo Cheong Khoo. "Dynamics of unsteady cavitating flow in compressible two-phase fluid." Ocean Engineering 87 (September 2014): 174–84. http://dx.doi.org/10.1016/j.oceaneng.2014.06.005.

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17

Romenski, Evgeniy, Dimitris Drikakis, and Eleuterio Toro. "Conservative Models and Numerical Methods for Compressible Two-Phase Flow." Journal of Scientific Computing 42, no. 1 (July 25, 2009): 68–95. http://dx.doi.org/10.1007/s10915-009-9316-y.

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18

MATSUSHITA, Shintaro, and Takayuki AOKI. "A Weakly Compressible Two-phase Flow Simulation on Cartesian Grids." Proceedings of The Computational Mechanics Conference 2017.30 (2017): 034. http://dx.doi.org/10.1299/jsmecmd.2017.30.034.

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19

Zeidan, D., E. Romenski, A. Slaouti, and E. F. Toro. "Numerical study of wave propagation in compressible two-phase flow." International Journal for Numerical Methods in Fluids 54, no. 4 (2007): 393–417. http://dx.doi.org/10.1002/fld.1404.

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20

Chen, Zhangxin. "Numerical Analysis for Two-phase Flow in Porous Media." Computational Methods in Applied Mathematics 3, no. 1 (2003): 59–75. http://dx.doi.org/10.2478/cmam-2003-0006.

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Abstract In this paper we derive error estimates for finite element approximations for partial differential systems which describe two-phase immiscible flows in porous media. These approximations are based on mixed finite element methods for pressure and velocity and characteristic finite element methods for saturation. Both incompressible and compressible flows are considered. Error estimates of optimal order are obtained.
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21

Guo, Yonghui, Ruo Li, and Chengbao Yao. "A Numerical Method on Eulerian Grids for Two-Phase Compressible Flow." Advances in Applied Mathematics and Mechanics 8, no. 2 (January 27, 2016): 187–212. http://dx.doi.org/10.4208/aamm.2014.m706.

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AbstractWe develop a numerical method to simulate a two-phase compressible flow with sharp phase interface on Eulerian grids. The scheme makes use of a levelset to depict the phase interface numerically. The overall scheme is basically a finite volume scheme. By approximately solving a two-phase Riemann problem on the phase interface, the normal phase interface velocity and the pressure are obtained, which is used to update the phase interface and calculate the numerical flux between the flows of two different phases. We adopt an aggregation algorithm to build cell patches around the phase interface to remove the numerical instability due to the breakdown of the CFL constraint by the cell fragments given by the phase interface depicted using the levelset function. The proposed scheme can handle problems with tangential sliping on the phase interface, topological change of the phase interface and extreme contrast in material parameters in a natural way. Though the perfect conservation of the mass, momentum and energy in global is not achieved, it can be quantitatively identified in what extent the global conservation is spoiled. Some numerical examples are presented to validate the numerical method developed.
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22

Daniels, L. C., C. P. Thompson, and C. Guardino. "AN IMPLICIT ONE-DIMENSIONAL TWO-PHASE COMPRESSIBLE FLOW SOLVER FOR PIPELINES." Multiphase Science and Technology 14, no. 2 (2002): 96. http://dx.doi.org/10.1615/multscientechn.v14.i2.10.

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23

Hansel, Joshua E., Ray A. Berry, David Andrs, Matthias S. Kunick, and Richard C. Martineau. "Sockeye: A One-Dimensional, Two-Phase, Compressible Flow Heat Pipe Application." Nuclear Technology 207, no. 7 (March 31, 2021): 1096–117. http://dx.doi.org/10.1080/00295450.2020.1861879.

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24

Amaziane, B., L. Pankratov, and A. Piatnitski. "Homogenization of immiscible compressible two–phase flow in random porous media." Journal of Differential Equations 305 (December 2021): 206–23. http://dx.doi.org/10.1016/j.jde.2021.10.012.

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25

Panfilov, M. B., Zh D. Baishemirov, and A. S. Berdyshev. "Macroscopic Model of Two-Phase Compressible Flow in Double Porosity Media." Fluid Dynamics 55, no. 7 (September 2020): 936–51. http://dx.doi.org/10.1134/s001546282007006x.

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26

Zayernouri, M., and M. J. Kermani. "DEVELOPMENT OF AN ANALYTICAL SOLUTION FOR COMPRESSIBLE TWO-PHASE STEAM FLOW." Transactions of the Canadian Society for Mechanical Engineering 30, no. 2 (June 2006): 279–96. http://dx.doi.org/10.1139/tcsme-2006-0017.

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27

YAMAGUCHI, Satoshi, and B. SHIN. "High-Speed Flow Phenomena in Compressible Gas-Liquid Two-Phase Media." Proceedings of Conference of Kyushu Branch 2018.71 (2018): C12. http://dx.doi.org/10.1299/jsmekyushu.2018.71.c12.

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28

Murrone, Angelo, and Hervé Guillard. "A five equation reduced model for compressible two phase flow problems." Journal of Computational Physics 202, no. 2 (January 2005): 664–98. http://dx.doi.org/10.1016/j.jcp.2004.07.019.

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29

Hamidi, S., and M. J. Kermani. "Numerical solutions of compressible two-phase moist-air flow with shocks." European Journal of Mechanics - B/Fluids 42 (November 2013): 20–29. http://dx.doi.org/10.1016/j.euromechflu.2013.04.002.

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30

So, K. K., X. Y. Hu, and N. A. Adams. "Anti-diffusion interface sharpening technique for two-phase compressible flow simulations." Journal of Computational Physics 231, no. 11 (June 2012): 4304–23. http://dx.doi.org/10.1016/j.jcp.2012.02.013.

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31

Jurak, Mladen, Alexandre Koldoba, Andrey Konyukhov, and Leonid Pankratov. "Nonisothermal immiscible compressible thermodynamically consistent two-phase flow in porous media." Comptes Rendus Mécanique 347, no. 12 (December 2019): 920–29. http://dx.doi.org/10.1016/j.crme.2019.11.015.

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32

Chenoweth, D. R., and S. Paolucci. "Compressible flow of a two-phase fluid between finite vessels—I." International Journal of Multiphase Flow 16, no. 6 (November 1990): 1047–69. http://dx.doi.org/10.1016/0301-9322(90)90106-s.

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33

Chamkha, Ali J. "Compressible two-phase boundary-layer flow with finite particulate volume fraction." International Journal of Engineering Science 34, no. 12 (September 1996): 1409–22. http://dx.doi.org/10.1016/0020-7225(96)00037-7.

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34

Sun, Shuaihui, Pei Ren, Pengcheng Guo, Longgang Sun, and Xiaobo Zheng. "Influence of the Gas Model on the Performance and Flow Field Prediction of a Gas–Liquid Two-Phase Hydraulic Turbine." Energies 15, no. 17 (August 30, 2022): 6325. http://dx.doi.org/10.3390/en15176325.

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A two-phase hydraulic turbine’s performance and flow field were predicted under different Inlet Gas Volume Fractions (IGVF) with incompressible and compressible models, respectively. The calculation equation of equivalent head, hydraulic efficiency, and flow loss considering the expanding work of compressible gas were deduced based on the energy conservation equations. Then, the incompressible and compressible results, including the output power and flow fields, are compared and analyzed. The compressible gas model’s equivalent head, output power, and flow loss are higher than the incompressible model, but the hydraulic efficiency is lower. As the IGVF increases, the gas gradually diffuses from the blade’s working surface to its suction surface. The gas–liquid separation happens at the runner outlet in the compressible results due to the gas expansion. The area of the low-pressure zone in the incompressible results increases with the IGVF. However, it decreases with the IGVF in the compressible results. As the gas expands in the blade passage, it takes up more flow area, causing the high liquid velocity in the same passage. The runner’s inlet gas distribution affects the liquid flow angle, causing the inlet shock and high TKE areas, especially in the blade passage near the volute tongue. The high TKE area in the compressible results is larger than the incompressible results because the inlet impact loss and the liquid velocity in the blade passage are higher. This paper provides a reference for selecting gas models in the numerical simulation of two-phase hydraulic turbines.
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35

Kubo, Takayuki, Yoshihiro Shibata, and Kohei Soga. "On some two phase problem for compressible and compressible viscous fluid flow separated by sharp interface." Discrete and Continuous Dynamical Systems 36, no. 7 (March 2016): 3741–74. http://dx.doi.org/10.3934/dcds.2016.36.3741.

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36

Romenski, E., A. D. Resnyansky, and E. F. Toro. "Conservative hyperbolic formulation for compressible two-phase flow with different phase pressures and temperatures." Quarterly of Applied Mathematics 65, no. 2 (April 19, 2007): 259–79. http://dx.doi.org/10.1090/s0033-569x-07-01051-2.

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37

Attou, A., and J. M. Seynhaeve. "Computation of steady-state multiple choked compressible flow: an analytical solution for single-phase and two-phase two-component flow." Journal of Loss Prevention in the Process Industries 11, no. 4 (July 1998): 229–47. http://dx.doi.org/10.1016/s0950-4230(98)00007-2.

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38

Scheufler, Henning, and Johan Roenby. "TwoPhaseFlow: A Framework for Developing Two Phase Flow Solvers in OpenFOAM." OpenFOAM® Journal 3 (November 20, 2023): 200–224. http://dx.doi.org/10.51560/ofj.v3.80.

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We present a new OpenFOAM based open-source framework, TwoPhaseFlow, enabling fast implementation and testing of new phase change and surface tension force models for two-phase flows including interfacial heat and mass transfer. Capitalizing on the runtime-selection mechanism in OpenFOAM, the new models can easily be selected and benchmarked against analytical solutions and existing models. The framework currently includes the following three interface curvature calculation methods for surface tension: 1) the height function method, 2) the parabolic fit method and 3) the reconstructed distance function method. As for phase change, two models are available: 1) Interface heat resistance and 2) direct heat flux. These can be combined in three solvers: 1) InterFlow for isothermal, incompressible two-phase flow, 2) compressibleInterFlow for compressible, non-isothermal two-phase flow and 3) multiRegionPhaseChangeFlow for compressible, non-isothermal two-phase flow with conjugated heat transfer. By design, addition of new models and solvers is straightforward and users are encouraged to contribute their specific models, solvers, and validation cases to the library.
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39

Bruce Ralphin Rose, J., S. Dhanalakshmi, and G. R. Jinu. "Experimental and numerical analysis of compressible two-phase flows in a shock tube." International Journal of Modeling, Simulation, and Scientific Computing 06, no. 03 (September 2015): 1550025. http://dx.doi.org/10.1142/s1793962315500257.

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The comparative study on seven equation models with two different six equations model for compressible two-phase flow analysis is proposed. The seven equations model is derived for compressible two-phase flow that is in the nonconservation form. In the present work, two different six equations model are derived for two pressures, two velocities and single temperature with the derivation of the equation of state. The closing equation for one of the six equations model is energy conservation equation while another one is closed by entropy balance equation. The partial differential form of governing equations is hyperbolic and written in the conservative form. At this point, the set of governing equations are derived based on the principle of extended thermodynamics. The method of solving single temperature from both six equation models are simple and direct solution can be obtained. Numerical simulation has been tried using one of the six equation models for air–water shock tube problems. Explicit fourth order Runge–Kutta scheme is used with Finite Volume Shock Capturing method for solving the governing equations numerically. The pressure, velocity and volume fraction variations are captured along the shock tube length through flow solver. Experimental work is carried out to magnify the initial stage of liquid injection into a gas. The outcome of six equations model for compressible two-phase flow has revealed the multi-phase flow characteristics that are similar to the actual conditions.
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40

Shokri, Vahid, and Kazem Esmaeili. "Effect of liquid phase compressibility on modeling of gas-liquid two-phase flows using two-fluid model." Thermal Science 23, no. 5 Part B (2019): 3003–13. http://dx.doi.org/10.2298/tsci171018148s.

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In this paper, a numerical study is performed in order to investigate the effect of the liquid phase compressibility two-fluid model. The two-fluid model is solved by using conservative shock capturing method. At the first, the two-fluid model is applied by assuming that the liquid phase is incompressible, then it is assumed that in three cases called water faucet case, large relative velocity shock pipe case, and Toumi?s shock pipe case, the liquid phase is compressible. Numerical results indicate that, if an intense pressure gradient is governed on the fluid-flow, single-pressure two-fluid model by assuming liquid phase incompressibility predicts the flow variables in the solution field more accurate than single-pressure two-fluid model by assuming liquid phase compressibility.
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41

McNeil, D. A. "Two-phase flow in orifice plates and valves." Proceedings of the Institution of Mechanical Engineers, Part C: Journal of Mechanical Engineering Science 214, no. 5 (May 1, 2000): 743–56. http://dx.doi.org/10.1243/0954406001523740.

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The pressure drop that occurs when a two-phase flow passes through a pipeline component is usually found by calculating the single-phase value and multiplying it by a two-phase multiplier. Little or no consideration is given to what occurs within that component. For example, if the valve seat area is sufficiently small, the fluid velocity will approach, or even reach, the critical velocity. In these circumstances, compressibility effects should be accounted for—they rarely are. This study was initiated to develop a technique that would allow pressure drops to be predicted for pipe fittings, whether the flow is compressible or not, and to allow the critical mass flux to be estimated, thus allowing the method to be applied to the design of venting systems. The model developed can be used for all pipe fittings of the contraction-expansion type, like orifice plates and valves, up to and including the choking point, provided the single-phase loss coefficient is known.
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42

MINATO, Akihiko. "Numerical Analysis of Gas-Liquid Two-Phase Flow by Using Compressible Two-Fluid Model." Transactions of the Japan Society of Mechanical Engineers Series B 68, no. 673 (2002): 2489–95. http://dx.doi.org/10.1299/kikaib.68.2489.

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43

Abed, Fayadh M., and Ghazi Y. Mohammed. "Assessment of Two-Phase Flow in a Venture Convergent- Divergent Nozzle." Tikrit Journal of Engineering Sciences 15, no. 2 (June 30, 2008): 17–31. http://dx.doi.org/10.25130/tjes.15.2.02.

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The present study emphasized on the information of cavitations during the dual phase flow i.e. (water and vapor) in venture converge-diverge nozzle. The choice of nozzle with a transparent material (PMMA), was found suitable for the observation and measurements. The model of this problem of defining dual compressible viscous flow, and k-epsilon model. The comparisons of numerical calculation and experimental observation were found to be comparatively coincidable in cavitational zone and throat pressure, and fractional phase flow.
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44

Bussac, Jean. "Study of relaxation processes in a two-phase flow model." ESAIM: Proceedings and Surveys 72 (2023): 2–18. http://dx.doi.org/10.1051/proc/202372002.

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This work concerns the analysis of the relaxation processes toward thermodynamical equilibrium arising in a compressible immiscible two-phase flow. Classically the relaxation processes are taken into account through dynamical systems which are coupled to the dynamics of the flow. The present paper compares two types of source terms which are commonly used: a BGK-like system and a mixture entropy gradient type. For both systems, main properties are investigated (agreement with second principle of thermodynamics, existence of solutions, maximum principle,...) and numerical experiments illustrate their asymptotic behaviour.
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45

Bedrikovetskii, P. G., E. V. Manevich, and R. �sedulaev. "Two-phase displacement of compressible fluids from stratified reservoirs." Fluid Dynamics 28, no. 2 (1993): 214–22. http://dx.doi.org/10.1007/bf01051210.

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46

Hérard, J. M., and H. Mathis. "A three-phase flow model with two miscible phases." ESAIM: Mathematical Modelling and Numerical Analysis 53, no. 4 (July 2019): 1373–89. http://dx.doi.org/10.1051/m2an/2019028.

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The paper concerns the modelling of a compressible mixture of a liquid, its vapor and a gas. The gas and the vapor are miscible while the liquid is immiscible with the gaseous phases. This assumption leads to non symmetric constraints on the void fractions. We derive a three-phase three-pressure model endowed with an entropic structure. We show that interfacial pressures are uniquely defined and propose entropy-consistent closure laws for the source terms. Naturally one exhibits that the mechanical relaxation complies with Dalton’s law on the phasic pressures. Then the hyperbolicity and the eigenstructure of the homogeneous model are investigated and we prove that it admits a symmetric form leading to a local existence result. We also derive a barotropic variant which possesses similar properties.
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47

García-Cascales, J. R., and H. Paillère. "Application of AUSM schemes to multi-dimensional compressible two-phase flow problems." Nuclear Engineering and Design 236, no. 12 (June 2006): 1225–39. http://dx.doi.org/10.1016/j.nucengdes.2005.11.013.

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48

Oladyshkin, S., and M. Panfilov. "Open thermodynamic model for compressible multicomponent two-phase flow in porous media." Journal of Petroleum Science and Engineering 81 (January 2012): 41–48. http://dx.doi.org/10.1016/j.petrol.2011.12.001.

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49

Ansari, M. R., and A. Daramizadeh. "Numerical simulation of compressible two-phase flow using a diffuse interface method." International Journal of Heat and Fluid Flow 42 (August 2013): 209–23. http://dx.doi.org/10.1016/j.ijheatfluidflow.2013.02.003.

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50

Kou, Jisheng, Shuyu Sun, and Xiuhua Wang. "Linearly Decoupled Energy-Stable Numerical Methods for Multicomponent Two-Phase Compressible Flow." SIAM Journal on Numerical Analysis 56, no. 6 (January 2018): 3219–48. http://dx.doi.org/10.1137/17m1162287.

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