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Journal articles on the topic 'Two- and three-phase flow'

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1

Zheng, Ying. "Ultrasonic Measurement for Two/Three-Phase Flow Detection." Canadian Journal of Chemical Engineering 81, no. 2 (2008): 268–70. http://dx.doi.org/10.1002/cjce.5450810212.

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2

Hérard, J. M., and H. Mathis. "A three-phase flow model with two miscible phases." ESAIM: Mathematical Modelling and Numerical Analysis 53, no. 4 (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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3

Risebro, Nils Henrik. "Three Models for Two Phase Flow in Porous Media." Vietnam Journal of Mathematics 47, no. 4 (2019): 835–49. http://dx.doi.org/10.1007/s10013-019-00367-1.

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4

Celata, G. P., M. Cumo, F. D'Annibale, and G. E. Farello. "Two-phase flow models in unbounded two-phase critical flows." Nuclear Engineering and Design 97, no. 2 (1986): 211–22. http://dx.doi.org/10.1016/0029-5493(86)90109-3.

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5

Liu, Shuhong, Yulin Wu, Yu Xu, and Hua-Shu Dou. "Analysis of Two-Phase Cavitating Flow with Two-Fluid Model Using Integrated Boltzmann Equations." Advances in Applied Mathematics and Mechanics 5, no. 05 (2013): 607–38. http://dx.doi.org/10.4208/aamm.12-m1256.

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AbstractIn the present work, both computational and experimental methods are employed to study the two-phase flow occurring in a model pump sump. The two-fluid model of the two-phase flow has been applied to the simulation of the three-dimensional cavitating flow. The governing equations of the two-phase cavitating flow are derived from the kinetic theory based on the Boltzmann equation. The isotropic RNGk — ε — kcaturbulence model of two-phase flows in the form of cavity number instead of the form of cavity phase volume fraction is developed. The RNGk—ε—kcaturbulence model, that is the RNGk — eturbulence model for the liquid phase combined with thekcamodel for the cavity phase, is employed to close the governing turbulent equations of the two-phase flow. The computation of the cavitating flow through a model pump sump has been carried out with this model in three-dimensional spaces. The calculated results have been compared with the data of the PIV experiment. Good qualitative agreement has been achieved which exhibits the reliability of the numerical simulation model.
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6

Blunt, M. J., and M. A. Christie. "Theory of Viscous Fingering in Two Phase, Three Component Flow." SPE Advanced Technology Series 2, no. 02 (1994): 52–60. http://dx.doi.org/10.2118/22613-pa.

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7

Spedding, P. L., E. Benard, and G. M. Mcnally. "Two- and Three-Phase Flow Through a 90 Degree Bend." Developments in Chemical Engineering and Mineral Processing 13, no. 5-6 (2008): 719–30. http://dx.doi.org/10.1002/apj.5500130521.

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8

Nagel, Tim, Julien Chauchat, Cyrille Bonamy, Xiaofeng Liu, Zhen Cheng, and Tian-Jian Hsu. "Three-dimensional scour simulations with a two-phase flow model." Advances in Water Resources 138 (April 2020): 103544. http://dx.doi.org/10.1016/j.advwatres.2020.103544.

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9

Alipchenkov, V. M., R. I. Nigmatulin, S. L. Soloviev, O. G. Stonik, L. I. Zaichik, and Y. A. Zeigarnik. "A three-fluid model of two-phase dispersed-annular flow." International Journal of Heat and Mass Transfer 47, no. 24 (2004): 5323–38. http://dx.doi.org/10.1016/j.ijheatmasstransfer.2004.07.011.

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10

Hassan, Y. A., William Schmidl, and J. Ortiz-Villafuerte. "Investigation of three-dimensional two-phase flow structure in a bubbly pipe flow." Measurement Science and Technology 9, no. 3 (1998): 309–26. http://dx.doi.org/10.1088/0957-0233/9/3/003.

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11

MURATA, Shigeto, Akihiko MINATO, and Osamu YOKOMIZO. "Calculation for Three-Dimensional Structures of Two-Phase Flow in Enlarged Flow Area." Journal of Nuclear Science and Technology 26, no. 9 (1989): 893–96. http://dx.doi.org/10.1080/18811248.1989.9734402.

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12

Zazovskii, A. F. "Two-phase three-component flow through a porous medium with variable total flow." Fluid Dynamics 20, no. 3 (1985): 433–39. http://dx.doi.org/10.1007/bf01049998.

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13

OCHI, Junji, Kyozo AYUKAWA, and Yoshihiro KADOTA. "Three-layer model analysis on two-phase critical flow through a conerging nozzle. On the case of two-component two-phase flow." Transactions of the Japan Society of Mechanical Engineers Series B 57, no. 536 (1991): 1232–38. http://dx.doi.org/10.1299/kikaib.57.1232.

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14

Krawczyk, John. "Two Phases, Three Runs." Mechanical Engineering 123, no. 10 (2001): 74–75. http://dx.doi.org/10.1115/1.2001-oct-7.

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Premcor Port Arthur Refinery, part of the Premcor Refining Group has been expanding the capacity of a vacuum tower processing almost one million pounds per hour of heavy hydrocarbon feed. The feed is deficient in lighter, more volatile components and is extremely viscous at room temperature. The process is intended to squeeze as much useful fuel as practical out of the oil feed. During the past 5 years, CFD has become noticeably more widespread in solving single-phase flow problems, but progress in solving multiphase flows has been much slower. There are at least three primary solution methods currently available to solve a dispersed multiphase flow problem. The contract with Premcor called for the use of a Eulerian method. Later, as an in-house test, Flow Simulations studied the model of the tower using two other methods.
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15

Naung, Khine Tun, Hayato TAJIMA, and Hideaki MONJI. "315 Analytical Study on Supersonic Two-Phase Flow Nozzle." Proceedings of Ibaraki District Conference 2012.20 (2012): 85–86. http://dx.doi.org/10.1299/jsmeibaraki.2012.20.85.

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16

Cueto-Felgueroso, Luis, and Ruben Juanes. "A phase-field model of two-phase Hele-Shaw flow." Journal of Fluid Mechanics 758 (October 9, 2014): 522–52. http://dx.doi.org/10.1017/jfm.2014.512.

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AbstractWe propose a continuum model of two-phase flow in a Hele-Shaw cell. The model describes the multiphase three-dimensional flow in the cell gap using gap-averaged quantities such as fluid saturation and Darcy flux. Viscous and capillary coupling between the fluids in the gap leads to a nonlinear fractional flow function. Capillarity and wetting phenomena are modelled within a phase-field framework, designing a heuristic free energy functional that induces phase segregation at equilibrium. We test the model through the simulation of bubbles and viscously unstable displacements (viscous fingering). We analyse the model’s rich behaviour as a function of capillary number, viscosity contrast and cell geometry. Including the effect of wetting films on the two-phase flow dynamics opens the door to exploring, with a simple two-dimensional model, the impact of wetting and flow rate on the performance of microfluidic devices and geological flows through fractures.
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17

TEZUKA, Akira, and Junichi Matsumoto. "Two-phase Flow Business?" Proceedings of the Fluids engineering conference 2005 (2005): 354. http://dx.doi.org/10.1299/jsmefed.2005.354.

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18

Ode, Kosuke, Toshihiro Ohmae, Kenji Yoshida, and Isao Kataoka. "STUDY OF FLOW STRUCTURE IN THE AERATION TANK INDUCED BY TWO PHASE JET FLOW(Multiphase Flow)." Proceedings of the International Conference on Jets, Wakes and Separated Flows (ICJWSF) 2005 (2005): 229–34. http://dx.doi.org/10.1299/jsmeicjwsf.2005.229.

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19

Deng, Bin, Chang Bo Jiang, Zhi Xin Guan, and Chao Shen. "Verification of STACS-VOF Based Two-Phase Flow Model for Interfacial Flows." Applied Mechanics and Materials 212-213 (October 2012): 1098–102. http://dx.doi.org/10.4028/www.scientific.net/amm.212-213.1098.

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The numerical calculation and simulation of gas-liquid two-phase flows with interfacial deformations have nowadays become more and more popular issues in various scientific and industrial fields. In this study, a three-dimensional gas-liquid two-phase flow numerical model is presented for investigating interfacial flows. The finite volume method was used to discretize the governing equations. A High-resolution scheme of VOF method (STACS) is applied to capture the free surface. The paper outlines the methodology of STACS and its validation against three typical test cases used to verify its accuracy. The results show the STACS-VOF gives very satisfactory results for three-dimensional two-phase interfacial flows problem, and this scheme performs more accurate and less diffusive preserving interface sharpness and boundedness.
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20

Sassi, Paolo, Youssef Stiriba, Julia Lobera, Virginia Palero, and Jordi Pallarès. "Experimental Analysis of Gas–Liquid–Solid Three-Phase Flows in Horizontal Pipelines." Flow, Turbulence and Combustion 105, no. 4 (2020): 1035–54. http://dx.doi.org/10.1007/s10494-020-00141-1.

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AbstractThe dynamics of three-phase flows involves phenomena of high complexity whose characterization is of great interest for different sectors of the worldwide industry. In order to move forward in the fundamental knowledge of the behavior of three-phase flows, new experimental data has been obtained in a facility specially designed for flow visualization and for measuring key parameters. These are (1) the flow regime, (2) the superficial velocities or rates of the individual phases; and (3) the frictional pressure loss. Flow visualization and pressure measurements are performed for two and three-phase flows in horizontal 30 mm inner diameter and 4.5 m long transparent acrylic pipes. A total of 134 flow conditions are analyzed and presented, including plug and slug flows in air–water two-phase flows and air–water-polypropylene (pellets) three-phase flows. For two-phase flows the transition from plug to slug flow agrees with the flow regime maps available in the literature. However, for three phase flows, a progressive displacement towards higher gas superficial velocities is found as the solid concentration is increased. The performance of a modified Lockhart–Martinelli correlation is tested for predicting frictional pressure gradient of three-phase flows with solid particles less dense than the liquid.
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21

Hibiki, Takashi, Joshua P. Schlegel, Tetsuhiro Ozaki, Shuichiro Miwa, and Somboon Rassame. "Simplified two-group two-fluid model for three-dimensional two-phase flow Computational Fluid Dynamics for vertical upward flow." Progress in Nuclear Energy 108 (September 2018): 503–16. http://dx.doi.org/10.1016/j.pnucene.2017.12.003.

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22

Louaked, M. "Well-posedness of incompressible models of two- and three-phase flow." IMA Journal of Applied Mathematics 68, no. 6 (2003): 595–620. http://dx.doi.org/10.1093/imamat/68.6.595.

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23

Spedding, P. L., G. S. Woods, R. S. Raghunathan, and J. K. Watterson. "Vertical Two-Phase Flow." Chemical Engineering Research and Design 76, no. 5 (1998): 620–27. http://dx.doi.org/10.1205/026387698525144.

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24

Spedding, P. L., G. S. Woods, R. S. Raghunathan, and J. K. Watterson. "Vertical Two-Phase Flow." Chemical Engineering Research and Design 76, no. 5 (1998): 628–34. http://dx.doi.org/10.1205/026387698525153.

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25

Spedding, P. L., G. S. Woods, R. S. Raghunathan, and J. K. Watterson. "Vertical Two-Phase Flow." Chemical Engineering Research and Design 76, no. 5 (1998): 612–19. http://dx.doi.org/10.1205/026387698525298.

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26

Woods, G. S., P. L. Spedding, J. K. Watterson, and R. S. Raghunathan. "Vertical Two Phase Flow." Developments in Chemical Engineering and Mineral Processing 7, no. 1-2 (2008): 7–16. http://dx.doi.org/10.1002/apj.5500070103.

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27

Elias, E., and G. S. Lellouche. "Two-phase critical flow." International Journal of Multiphase Flow 20 (August 1994): 91–168. http://dx.doi.org/10.1016/0301-9322(94)90071-x.

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28

Brand, B., R. Emmerling, Ch Fischer, H. P. Gaul, and K. Umminger. "Two-phase flow instrumentation." Nuclear Engineering and Design 145, no. 1-2 (1993): 113–30. http://dx.doi.org/10.1016/0029-5493(93)90062-e.

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29

Turza, J., Z. Tkáč, and M. Gullerová. "Geometric displacement volume and flow in the phase of a two-phase hydraulic converter." Research in Agricultural Engineering 53, No. 2 (2008): 54–66. http://dx.doi.org/10.17221/2122-rae.

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The paper researches the possibilities to replace the parallel flow hydraulic mechanisms in agricultural machinery with hydraulic units with fluid alternating flow as they provide more efficient operation due to their output alternating motion. The method being presented analyses how the geometric displacement volume in the fluid alternating piston converter is created. This is basically achieved by adding or omitting elements in the phase which consequently reduces the quantity of converter types being manufactured.
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30

He, Ping, Nai Chao Chen, and Dan Mei Hu. "Study of Wake Characteristics of a Horizontal-Axis Wind Turbine within Two-Phase Flow." Key Engineering Materials 474-476 (April 2011): 811–15. http://dx.doi.org/10.4028/www.scientific.net/kem.474-476.811.

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The two-phase flow is addressed for the more accurate estimation of the wake characteristic for the horizontal-axis wind turbine operating in the complexly unsteady environmental states. The computational fluid dynamics (CFD) method is implemented for performing the three-dimensional wind turbine using the simulating software tool of FLUNT. Three types of environmental states, single-phase flow, liquid-gas flow and solid-gas flow, are performed for the comparison of velocity and pressure distribution to derive the specify feature for wind turbine within two-phase flow environmental state. The calculated results shows that there has the similar evolutional tendency of velocity distribution for both single- and two-phase flows and the velocity decrement at the distance of 20 meter away from wind turbine still reach to 80% of inflow speed. But the turbine blade within two-phase flow is subject to the unsteady flow with the larger velocity gradient compared with that within single-phase flow. For the static pressure, large difference occurred in these three types of environmental state reveals that the second material in addition to atmospheres causes the prominent influence of aerodynamic force and its power coefficient. The results exhibit that wind turbine within solid-gas flow has the largest power coefficient that those within the gas and liquid-gas flows.
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31

Petrovic, Milan, and Vladimir Stevanovic. "Two-component two-phase critical flow." FME Transaction 44, no. 2 (2016): 109–14. http://dx.doi.org/10.5937/fmet1602109p.

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32

MURATA, Shigeto, Akihiko MINATO, and Osamu YOKOMIZO. "Development of Three-Dimensional Analysis Code for Two-Phase Flow Using Two-Fluid Model." Journal of Nuclear Science and Technology 28, no. 11 (1991): 1029–40. http://dx.doi.org/10.1080/18811248.1991.9731466.

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33

Sharma, Subash L., Mamoru Ishii, Takashi Hibiki, Joshua P. Schlegel, Yang Liu, and John R. Buchanan. "Beyond bubbly two-phase flow investigation using a CFD three-field two-fluid model." International Journal of Multiphase Flow 113 (April 2019): 1–15. http://dx.doi.org/10.1016/j.ijmultiphaseflow.2018.12.010.

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34

HARAGUCHI, Naoki, and Hiroyasu OHTAKE. "ICONE19-43620 Study on Pressure Loss of Liquid Single-Phase Flow and Two Phase Flow in Micro- and Mini-Channels." Proceedings of the International Conference on Nuclear Engineering (ICONE) 2011.19 (2011): _ICONE1943. http://dx.doi.org/10.1299/jsmeicone.2011.19._icone1943_250.

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35

Triplett, K. A., S. M. Ghiaasiaan, S. I. Abdel-Khalik, and D. L. Sadowski. "Gas–liquid two-phase flow in microchannels Part I: two-phase flow patterns." International Journal of Multiphase Flow 25, no. 3 (1999): 377–94. http://dx.doi.org/10.1016/s0301-9322(98)00054-8.

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36

Kurreck, M., M. Willmann, and S. Wittig. "Prediction of the Three-Dimensional Reacting Two-Phase Flow Within a Jet-Stabilized Combustor." Journal of Engineering for Gas Turbines and Power 120, no. 1 (1998): 77–83. http://dx.doi.org/10.1115/1.2818090.

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Numerical calculations of the two-phase flow in an experimentally well-investigated research combustor are presented. The comparison between measurements and calculations demonstrates the capabilities of the state-of-the-art Euler/Lagrange method for calculating two-phase flows, when applied to a complex reacting liquid-fueled combustor. The governing equations for gaseous and liquid phase are presented, with special emphasis on the control of the coupling process between the two phases. The relaxation method employed, together with a convergence history, shows a suitable way to achieve a fast and accurate solution for the strongly coupled two-phase flow under investigation. Furthermore, methods are presented to simulate the stochastic behavior of the atomization process caused by an air-blast atomizer. In addition to the numerical methods, experimental techniques are presented that deliver detailed information about droplet starting conditions.
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37

Tomiyama, Akio, Hisato Minagawa, Naoya Furutani, and Tadashi Sakaguchi. "Application of a Two-Phase Flow Model based on Local Relative Velocity to Gas-Liquid-Solid Three-Phase Flow." Transactions of the Japan Society of Mechanical Engineers Series B 59, no. 561 (1993): 1545–52. http://dx.doi.org/10.1299/kikaib.59.1545.

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38

Voutsinas, Alexandros, Toshihiko Shakouchi, Junichi Takamura, Koichi Tsujimoto, and Toshitake Ando. "FLOW AND CONTROL OF VERTICAL UPWARD GAS-LIQUID TWO-PHASE FLOW THROUGH SUDDEN CONTRACTION PIPE(Multiphase Flow 2)." Proceedings of the International Conference on Jets, Wakes and Separated Flows (ICJWSF) 2005 (2005): 307–12. http://dx.doi.org/10.1299/jsmeicjwsf.2005.307.

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39

UEMATSU, Junichi, Kazuya ABE, Tatsuya HAZUKU, Tomoji TAKAMASA, and Takashi HIBIKI. "ICONE15-10315 EFFECT OF WALL WETTABILITY ON FLOW CHARACTERISTICS OF GAS-LIQUID TWO-PHASE FLOW." Proceedings of the International Conference on Nuclear Engineering (ICONE) 2007.15 (2007): _ICONE1510. http://dx.doi.org/10.1299/jsmeicone.2007.15._icone1510_159.

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40

Frankum, D. P., V. V. Wadekar, and B. J. Azzopardi. "Two-phase flow patterns for evaporating flow." Experimental Thermal and Fluid Science 15, no. 3 (1997): 183–92. http://dx.doi.org/10.1016/s0894-1777(97)00020-4.

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41

Oddie, Gary, and J. R. Anthony Pearson. "FLOW-RATE MEASUREMENT IN TWO-PHASE FLOW." Annual Review of Fluid Mechanics 36, no. 1 (2004): 149–72. http://dx.doi.org/10.1146/annurev.fluid.36.050802.121935.

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42

Chen, S. S. "Flow-Induced Vibrations in Two-Phase Flow." Journal of Pressure Vessel Technology 113, no. 2 (1991): 234–41. http://dx.doi.org/10.1115/1.2928751.

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Two-phase flow exists in many shell-and-tube heat exchangers and power generation components. The flowing fluid is a source of energy that can induce small-amplitude subcritical oscillations and large-amplitude dynamic instabilities. In fact, many practical system components have experienced excessive flow-induced vibrations. This paper reviews the current understanding of vibration of circular cylinders in quiescent fluid, cross-flow, and axial flow, with emphasis on excitation mechanisms, mathematical models, and available experimental data. A unified theory is presented for cylinders oscillating under different flow conditions.
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43

Seeger, M. "Coriolis flow measurement in two phase flow." Computing and Control Engineering 16, no. 3 (2005): 10–16. http://dx.doi.org/10.1049/cce:20050301.

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44

McQuillan, K. W., and P. B. Whalley. "Flow patterns in vertical two-phase flow." International Journal of Multiphase Flow 11, no. 2 (1985): 161–75. http://dx.doi.org/10.1016/0301-9322(85)90043-6.

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45

Rahman, M. M., Nobuatsu Tanaka, S. Yokobori, and S. Hirai. "Three Dimensional Numerical Analysis of Two Phase Flow Separation Using Swirling Fluidics." Energy and Power Engineering 05, no. 04 (2013): 301–6. http://dx.doi.org/10.4236/epe.2013.54030.

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46

Aghaee, Mohammad, Rouhollah Ganjiazad, Ramin Roshandel, and Mohammad Ali Ashjari. "Two-phase flow separation in axial free vortex flow." Journal of Computational Multiphase Flows 9, no. 3 (2017): 105–13. http://dx.doi.org/10.1177/1757482x17699411.

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Multi-phase flows, particularly two-phase flows, are widely used in the industries, hence in order to predict flow regime, pressure drop, heat transfer, and phase change, two-phase flows should be studied more precisely. In the petroleum industry, separation of phases such as water from petroleum is done using rotational flow and vortices; thus, the evolution of the vortex in two-phase flow should be considered. One method of separation requires the flow to enter a long tube in a free vortex. Investigating this requires sufficient knowledge of free vortex flow in a tube. The present study examined the evolution of tube-constrained two-phase free vortex using computational fluid dynamics. The discretized equations were solved using the SIMPLE method. It was determined that as the liquid flows down the length of the pipe, the free vortex evolves into combined forced and free vortices. The tangential velocity of the free and forced vortices also decreases in response to viscosity. It is shown that the concentration of the second discrete phase (oil) is greatest at the center of the pipe in the core of the vortex. This concentration is at a maximum at the outlet of the pipe.
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47

Kichatov, B. V., and I. V. Boyko. "Two-Phase Flow with Phase Transitions Instability." Heat Transfer Research 28, no. 4-6 (1997): 273–76. http://dx.doi.org/10.1615/heattransres.v28.i4-6.80.

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48

PROSPERETTI, A., and D. Z. ZHANG. "DISPERSE PHASE STRESS IN TWO-PHASE FLOW." Chemical Engineering Communications 141-142, no. 1 (1996): 387–98. http://dx.doi.org/10.1080/00986449608936425.

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49

Tracy, F. T. "One-, two-, and three-dimensional solutions for counter-current steady-state two-phase subsurface flow." International Journal of Multiphase Flow 34, no. 5 (2008): 437–46. http://dx.doi.org/10.1016/j.ijmultiphaseflow.2007.02.011.

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50

Ebner, Lothar, and Marie Fialová. "On Instabilities in Horizontal Two-Phase Flow." Collection of Czechoslovak Chemical Communications 59, no. 12 (1994): 2595–603. http://dx.doi.org/10.1135/cccc19942595.

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Two regions of instabilities in horizontal two-phase flow were detected. The first was found in the transition from slug to annular flow, the second between stratified and slug flow. The existence of oscillations between the slug and annular flows can explain the differences in the limitation of the slug flow in flow regime maps proposed by different authors. Coexistence of these two regimes is similar to bistable behaviour of some differential equation solutions.
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