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Relevant bibliographies by topics / Two- and three-phase flow

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Academic literature on the topic 'Two- and three-phase flow'

Author: Grafiati

Published: 4 June 2021

Last updated: 1 February 2022

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

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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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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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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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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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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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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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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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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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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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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Dissertations / Theses on the topic "Two- and three-phase flow"

1

Sukarno, Pudjo. "Inflow performance relationship curves in two-phase and three-phase flow conditions /." Access abstract and link to full text, 1986. http://0-wwwlib.umi.com.library.utulsa.edu/dissertations/fullcit/8614191.

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Akbar, Muhammad Khalid. "Transport Phenomena in Complex Two and Three-Phase Flow Systems." Diss., Georgia Institute of Technology, 2004. http://hdl.handle.net/1853/4897.

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Two and three-phase flow processes involving gas, liquid and solid, are common in nature and industry, and include some of the most complex and poorly-understood transport problems. In this research hydrodynamics, heat and mass transfer processes in complex two and three-phase flows were investigated. The interfacial surface area concentration in a short vertical column subject to the through flow of fiber-liquid-gas slurry was experimentally measured using the gas absorption technique. The experimental data were statistically analyzed for parametric effects, and were empirically correlated. The absorption of a gaseous species by a slurry droplet with internal circulation and containing reactive micro-particles was simulated, and parametrically studied. The micro-particles were found to enhance the absorption rate. The absorption rate was sensitive to droplet recirculation, and shrinkage of particles with time resulted in declining absorption rates. The transport of soot particles, suspended in laminar hot gas flowing in a tube, was modeled and parametrically studied. Due to coupled thermal radiation and thermophoresis, a radially-nonuniform temperature profile develops, leading to sharp, non-uniform radial soot-concentration profiles. The assumption of monodisperse particles leads to over-prediction of thermophoresis. The transport and removal of particles suspended in bubbles rising in a stagnant liquid pool were modeled based on a Eulerian – Monte Carlo method. The bubble hydrodynamics were treated in Eulerian frame, using the Volume-of-Fluid (VOF) technique, while particle equations of motion were numerically solved in Lagrangian frame. The bubbles undergo shape change, and have complex internal circulation, all of which influence the particle removal. Model predictions were also compared with experimental data. Using a resemblance between two-phase flow in microchannels, and in large channels at microgravity, a simple Weber number-based two-phase flow regime map was developed for microchannels. Based on the available air-water experimental data, a criterion for the prediction of conditions that lead to flow regime transition out of the stratified-wavy flow pattern in horizontal annular channels was proposed. The thermocapillary effects on liquid-vapor interface shape during heterogeneous bubble ebullition in microchannels were analytically studied.

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Kunda, Wilkinson. "Two phase problems and two phase flow." Thesis, University of Hull, 1986. http://hydra.hull.ac.uk/resources/hull:5902.

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In section 1 of this thesis a two-dimensional mathematical model is used to investigate the circulation in a gas-bubble agitation system of a cylindrical vessel for the case of an orifice located at the centre of the base. The two-phase (liquid/gas) region is assumed to be confined to a cone-shaped region and is investigated using Wallis' Drift Flux Model. In the single-phase (liquid) region the turbulent Navier-Stokes equations, written in terms of the stream function, are used for the mathematical model. The analysis in the two-phase region yields the boundary conditions on the two-phase/single-phase boundary. The velocity field in the two-phase region is solved analytically giving results in closed form. A numerical algorithm is developed for calculating liquid flow in the single phase region, and numerical results are presented graphically in terms of the stream function. In section 2 two moving interface problems are investigated. Small time analytic solutions are found for three-dimensional inward solidification of a half space initially at fusion temperature in the first problem. In the second problem, perturbation solutions for melting of a cylindrical annulus with constant heat flux on inner surface are given. In both problems the interface immobilization technique is used. Interface locations at various times are calculated for the inward solidification problem and the results shown in three-dimensional graphs. First and second perturbation terms for the interface location are given for the second problem and graphs of each are presented for a particular case.

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Rapisarda, Andrea. "Hydrodynamic characterization of two/three phase flow regimes in stirred tank." Master's thesis, Alma Mater Studiorum - Università di Bologna, 2019.

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Questo progetto di ricerca riguarda i processi di miscelazione in sistemi multifase meccanicamente agitati(regime turbolento). I sistemi studiati sono: gas-liquido, solido-liquido e gas-solido-liquido. Lo scopo è quello di analizzare il movimento delle particelle solide all'interno di un recipiente agitato, calcolandone la velocità(n) alle quali si è ottenuto lo stato di estrazione delle particelle(nJD), della completa dispersione(nCD) e del loading(nloading), attraverso l'uso di due diversi valori di diametro delle particelle. Le misure sono state effettuate utilizzando due giranti su un albero e condotte con 6 diverse portate di gas e (da 3 a 6) concentrazioni X di particelle solide. La presente ricerca dimostra che i valori di nloading non dipendono dalla concentrazione X di particelle nel sistema con acqua come fase liquida per entrambi i diametri di particelle dp, nel sistema con 0.4 Kmol/m3 di NaCl per dp1 e nel sistema con 0.8 Kmol/m3 di NaCl per dp2. Nei sistemi con acqua e 0.4 Kmol/m3 di NaCl come fase liquida, i valori di nCD aumentano con l'aumento della concenrtrazione di particelle. I valori di nJD aumentano significamente con l'aumento della concentrazione solida, per entrambi i diametri di particelle nel sistema a coalescenza(con acqua) e non coalescenza con concentrazione di elettrolita 0.8 Kmol/m3 di NaCl. La stessa dipendenza di nJD=f(X) è osservata per 0.4 Kmol/m3 di NaCl per dp2. Per l'intera gamma di concentrazioni solide X, per lo stesso valore ddel diametro delle particelle, si ottengono valori inferiori di velocità di nloading, nCD, nJD per la configurazione delle giranti CD6-PBT.

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Ahmadi, Motlagh Amir Hossein. "CFD simulation of two- and three-phase flow in FCC reactors." Thesis, University of British Columbia, 2015. http://hdl.handle.net/2429/52621.

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Liquid distribution and evaporation in Fluid Catalytic Cracking (FCC) reactors are investigated numerically. The well-documented inaccuracy of conventional two-fluid modeling of hydrodynamics in fluidized beds of Geldart Group A particles is revisited. A new force-balance (FB) sub-grid-scale model, introduced and applied to the conventional Wen-Yu drag correlation, analyzes the balance of van der Waals, drag, gravity and buoyancy forces. It predicts formation of agglomerates inside the bed, updating the drag calculations by applying a correction factor to the conventional drag models. Good predictions are obtained of fluidization regimes and bed expansion, and there is promising agreement with experimental time-average radial voidage profiles reported by Dubrawski et al. (2013). Good quantitative agreement between discrete element models (DEM) and two-fluid predictions of minimum bubbling velocity is also observed when the model is used to predict minimum bubbling velocity, in contrast to the predictions from a non-cohesive, Wen-Yu model. Liquid injection experiments on a lab-scale fluidized bed were conducted, at the Institute of Chemical and Fuels from Alternative Sources (ICFAR) in London, Ontario to study the distribution, as well as the penetration, of liquid into catalyst pores. The results shed light on complexities involved in the injection zone to understand the effect of superficial gas velocity on evaporation and imbibition of liquid into particle pores. A methodology is developed to couple and incorporate existing liquid imbibition (into particle pores) models with evaporation models in the CFD code. The results are compared to another set of lab-scale experiments conducted at the British Columbia Research Institute (BCRI) facilities in Burnaby, BC. Simulation results demonstrate that CFD models can capture correct qualitative behavior of liquid injection and evaporation inside the bed. However, quantitative deviations revealed the likely effect of hydrodynamic properties on drying from both the liquid film around the particles and inside the pores. The deviations also imply that the assumption of convection- or diffusion-dominant drying might be unsuitable, and the two should be combined. Based on experimental results, a methodology is proposed to include the effect of hydrodynamic properties such as superficial gas velocity and particle impact velocity on drying.<br>Applied Science, Faculty of<br>Chemical and Biological Engineering, Department of<br>Graduate

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Jahanbakhsh, Amir. "Two- and three-phase flow functions for numerical simulation of EOR processes." Thesis, Heriot-Watt University, 2016. http://hdl.handle.net/10399/3218.

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The understanding of governing mechanisms of multi-phase (oil, water, and gas) flow in porous media is of keen interest in petroleum and environmental engineering. In the petroleum engineering context, three-phase flow occurs in several important processes including in enhanced oil recovery (EOR). Recovery of a significant amount of the residual oil in reservoirs after primary recovery and secondary recovery (waterflooding) is important in order to tackle the increasing demand for the energy. EOR methods mainly involve two and three-phase flow in the reservoir. Relative permeability (kr) and capillary pressure (Pc) are two important parameters in multiphase flow which describe the interaction of each fluid in porous media. The importance of these flow functions will be even more significant for three-phase flow systems. This thesis attempts to address three key issues. (i) Improved determination of multi-phase flow functions (kr and Pc). (ii) The impact of parameters affecting flow functions. (iii) Prediction of multi-phase flow functions. Relative permeability (kr) can be measured in the laboratory using steady-state and unsteady-state methods, or estimated by mathematical correlations and pore-network models. As multi-phase flow experiments and in particular steady-state measurements are very time consuming and expensive, more often the unsteady-state method is used for multi-phase kr measurements. In this thesis, a methodology has been devised for calculating kr values and in particular three-phase kr from unsteady-state experiments. The effort was extended to simultaneously calculating Pc from the same coreflood experiment. There are different physical parameters which can affect flow functions. The effect of gas/oil interfacial tension (IFTg/o) on two and three-phase kr and also on residual saturation during alternative water and gas injections has also been studied. Finally, two-phase kr have been estimated for rock and fluid conditions where there is no previous data. This has been achieved by taking data from different conditions under which measurements were made.

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Malhotra, Ajay. "Study of two and three-phase flows in large diameter horizontal pipelines." Ohio : Ohio University, 1995. http://www.ohiolink.edu/etd/view.cgi?ohiou1179947127.

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Ariyoshi, Gen. "Flow Characteristics of Lead-Bismuth Two-phase Flow." Kyoto University, 2019. http://hdl.handle.net/2433/242325.

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Makhlouf, Eliana Mary Seinfeld John H. Seinfeld John H. "Estimation of absolute permeability in multilayered petroleum reservoirs with two- and three-phase flow /." Diss., Pasadena, Calif. : California Institute of Technology, 1990. http://resolver.caltech.edu/CaltechETD:etd-03162007-091347.

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Isaacs, Steven. "Two-phase flow and heat transfer in pin-fin enhanced micro-gaps." Thesis, Georgia Institute of Technology, 2013. http://hdl.handle.net/1853/50282.

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In modern microprocessors, thermal management has become one of the main hurdles in continued performance enhancement. Cooling schemes utilizing single phase microfluidics have been investigated extensively for enhanced heat dissipation from microprocessors. However, two-phase fluidic cooling devices are becoming a promising approach, and are less understood. This study aims to examine two-phase flow and heat transfer within a pin-fin enhanced micro-gap. The pin-fin array covered an area of 1cm x 1cm and had a pin diameter, height and pitch of 150μm, 200μm and 225μm, respectively, (aspect ratio of 1.33). This study covers both uniformly and partially heated scenarios. The working fluid used was R245fa. The average heat transfer coefficient and high speed flow visualization results indicated a rapid transition to the annular flow regime with a strong dependence on heat flux. Also, unique, conically-shaped two-phase wakes were observed, demonstrating the lateral spreading capability of the pin-fin array geometry.

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Books on the topic "Two- and three-phase flow"

1

Peker, Sümer M. Solid-liquid two phase flow. Elsevier, 2008.

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Kakaç, Sadik, Arthur E. Bergles, and E. Oliveira Fernandes, eds. Two-Phase Flow Heat Exchangers. Springer Netherlands, 1988. http://dx.doi.org/10.1007/978-94-009-2790-2.

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Peker, Suemer M. Solid-liquid two phase flow. Elsevier Science Pub, 2008.

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Two-phase flow in complex systems. John Wiley, 1999.

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Teixeira, Jose Carlos Fernandes. Turbulence in annular two phase flow. University of Birmingham, 1988.

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Whalley, P. B. Two-phase flow and heat transfer. Oxford University Press, 1996.

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Wang, Yu-Jiun. Parameters of two-phase bubbly flow. University of Birmingham, 1999.

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Gu, Junjie, Shujun Wang, and Zhongxue Gan. Two-Phase Flow in Refrigeration Systems. Springer New York, 2014. http://dx.doi.org/10.1007/978-1-4614-8323-6.

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Coward, Adrian V. Stability of oscillatory two phase Couette flow. Institute for Computer Applications in Science and Engineering, 1993.

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Critical regimes of two-phase flows with a polydisperse solid phase. Springer, 2010.

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Book chapters on the topic "Two- and three-phase flow"

1

Bourgeat, Alain. "Two-Phase Flow." In Interdisciplinary Applied Mathematics. Springer New York, 1997. http://dx.doi.org/10.1007/978-1-4612-1920-0_5.

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Akimoto, Hajime, Yoshinari Anoda, Kazuyuki Takase, Hiroyuki Yoshida, and Hidesada Tamai. "Two-Phase Flow." In An Advanced Course in Nuclear Engineering. Springer Japan, 2016. http://dx.doi.org/10.1007/978-4-431-55603-9_11.

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Gray, William G., and Cass T. Miller. "Two-Phase Flow." In Advances in Geophysical and Environmental Mechanics and Mathematics. Springer International Publishing, 2014. http://dx.doi.org/10.1007/978-3-319-04010-3_11.

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Bruining, Hans. "Two-Phase Flow." In Upscaling of Single- and Two-Phase Flow in Reservoir Engineering. CRC Press, 2021. http://dx.doi.org/10.1201/9781003168386-4.

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Taylor, A. M. K. P. "Two Phase Flow Measurements." In Optical Diagnostics for Flow Processes. Springer US, 1994. http://dx.doi.org/10.1007/978-1-4899-1271-8_10.

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van Wijngaarden, L. "Turbulent Two-Phase Flow." In Advances in Turbulence VI. Springer Netherlands, 1996. http://dx.doi.org/10.1007/978-94-009-0297-8_154.

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Todreas, Neil E., and Mujid S. Kazimi. "Two-Phase Flow Dynamics." In Nuclear Systems Volume I. CRC Press, 2021. http://dx.doi.org/10.1201/9781351030502-11.

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Fasanino, Guy, and Jean-Eric Molinard. "Two-Phase Flow Simulation." In Underground Storage of Natural Gas. Springer Netherlands, 1989. http://dx.doi.org/10.1007/978-94-009-0993-9_19.

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Poinsot, Thierry. "Two-Phase Flow Combustion." In Instabilities of Flows: With and Without Heat Transfer and Chemical Reaction. Springer Vienna, 2010. http://dx.doi.org/10.1007/978-3-7091-0127-8_10.

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Osher, Stanley, and Ronald Fedkiw. "Two-Phase Compressible Flow." In Applied Mathematical Sciences. Springer New York, 2003. http://dx.doi.org/10.1007/0-387-22746-6_15.

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Conference papers on the topic "Two- and three-phase flow"

1

Anquez, P., M. Zakari, and G. Caumon. "Comparing Three DFN Simplification Strategies for Two-Phase Flow Applications." In ECMOR XVII. European Association of Geoscientists & Engineers, 2020. http://dx.doi.org/10.3997/2214-4609.202035112.

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Bărglăzan, M., C. Velescu, T. Miloş, A. Manea, E. Dobândă, and C. Stroiţă. "Hydrodynamic transmission operating with two-phase flow." In MULTIPHASE FLOW 2007. WIT Press, 2007. http://dx.doi.org/10.2495/mpf070361.

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Donnelly, G. F., P. L. Spedding, and W. J. McBride. "Prediction of Two and Three Phase Flow in the Horizontal Configuration." In Offshore Technology Conference. Offshore Technology Conference, 1995. http://dx.doi.org/10.4043/7743-ms.

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Dale, E. I., and A. Skauge. "Features Concerning Capillary Pressure and the Effect on Two-phase and Three-phase Flow." In IOR 2007 - 14th European Symposium on Improved Oil Recovery. European Association of Geoscientists & Engineers, 2007. http://dx.doi.org/10.3997/2214-4609-pdb.24.a19.

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Afgan, Naim Hamdia. "TRANSIENT TWO PHASE FLOW." In International Heat Transfer Conference 9. Begellhouse, 1990. http://dx.doi.org/10.1615/ihtc9.1820.

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Kourakos, V. G., P. Rambaud, S. Chabane, D. Pierrat, and J. M. Buchlin. "Two-phase flow modelling within expansion and contraction singularities." In MULTIPHASE FLOW 2009. WIT Press, 2009. http://dx.doi.org/10.2495/mpf090031.

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Popova, M., P. Vorobieff, and M. Ingber. "Analysis of two- and three-particle motion in a Couette cell." In MULTIPHASE FLOW 2007. WIT Press, 2007. http://dx.doi.org/10.2495/mpf070301.

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Li, Xintian, Hui Tian, Nanjia Yu, and Guobiao Cai. "Three-dimensional Numerical Simulation of Two-phase Flow in Hybrid Rocket Motor." In 49th AIAA/ASME/SAE/ASEE Joint Propulsion Conference. American Institute of Aeronautics and Astronautics, 2013. http://dx.doi.org/10.2514/6.2013-3893.

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Pal, Mayur, Sadok Lamine, Knut-Andreas Lie, and Stein Krogstad. "Multiscale Method for Simulating Two-and Three-Phase Flow in Porous Media." In SPE Reservoir Simulation Symposium. Society of Petroleum Engineers, 2013. http://dx.doi.org/10.2118/163669-ms.

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Yuan, Wenqi, and Suiqing Liu. "Three-Dimensional Numerical Modeling of Two-Phase Flow in Water-Filling Pipelines." In 12th Annual Conference on Water Distribution Systems Analysis (WDSA). American Society of Civil Engineers, 2011. http://dx.doi.org/10.1061/41203(425)13.

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Reports on the topic "Two- and three-phase flow"

1

Wallis, G. B. Two phase potential flow. Office of Scientific and Technical Information (OSTI), 1991. http://dx.doi.org/10.2172/6213215.

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Maeder, P. F., and J. Kestin. Two-phase flow in geothermal systems. Office of Scientific and Technical Information (OSTI), 1987. http://dx.doi.org/10.2172/5984665.

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Wallis, G. B. Two-Phase Potential Flow. Final report. Office of Scientific and Technical Information (OSTI), 1999. http://dx.doi.org/10.2172/761114.

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Farwagi, S. M. Computer Modelling of Two-Phase Flow. Defense Technical Information Center, 1986. http://dx.doi.org/10.21236/ada175048.

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Domokos, G., S. Kovesi-Domokos, and C. K. Zoltani. Boltzmann Equation Approach to Two-Phase Flow Turbulence. Defense Technical Information Center, 1988. http://dx.doi.org/10.21236/ada196153.

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Theilacker, Jay, and C. Rode. An Investigation Into Flow Regimes for Two Phase Helium Flow. Office of Scientific and Technical Information (OSTI), 1987. http://dx.doi.org/10.2172/1151469.

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Ishii, M., S. B. Kim, and R. Lee. Flow visualization study of inverted U-bend two-phase flow. Office of Scientific and Technical Information (OSTI), 1986. http://dx.doi.org/10.2172/6839281.

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Kuhlman, Kristopher, and Jason Heath. Multicontinuum Flow Models for Assessing Two-Phase Flow in Containment Science . Office of Scientific and Technical Information (OSTI), 2021. http://dx.doi.org/10.2172/1809129.

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Trabold, T. A., and R. Kumar. Vapor core turbulence in annular two-phase flow. Office of Scientific and Technical Information (OSTI), 1998. http://dx.doi.org/10.2172/353193.

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Kumar, R., and D. P. Edwards. Interfacial shear modeling in two-phase annular flow. Office of Scientific and Technical Information (OSTI), 1996. http://dx.doi.org/10.2172/350939.

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