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Journal articles on the topic 'Single and two-phase flow'

Author: Grafiati

Published: 3 June 2025

Last updated: 1 August 2025

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1

Dhruvkumar, Joshi, Sethi Upasna, and Tekwani Hardik. "Single and Two Phase Pressure Drop in Fluid." International Journal of Trend in Scientific Research and Development 2, no. 4 (2019): 394–97. https://doi.org/10.31142/ijtsrd12966.

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Pressure drop is of paramount importance in a fluid flow. Single phase pressure drop occurs in a pure liquid or pure gas flow. Two phase pressure drop occurs in phase changing equipments like evaporators and condensers of refrigeration air conditioning plants and heat pumps. Maximum two three types of pressure drop frictional, gravitational and acceleration can occur in a single or two phase flow. In each case, pressure drop take place in straight pipes. Several empirical equations and correlations have been developed and compared for the pressure drop. Consequently well planned pipe layout an

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2

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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3

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 (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 nat

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4

Babus'Haq, Ramiz, and S. Douglas Probert. "Natural circulation in single-phase and two-phase flow." Applied Energy 38, no. 4 (1991): 325–27. http://dx.doi.org/10.1016/0306-2619(91)90083-a.

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5

Lübke, Martin, and Olaf Wünsch. "Two-Phase Flow in Single-Screw Extruders." PAMM 12, no. 1 (2012): 509–10. http://dx.doi.org/10.1002/pamm.201210243.

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6

Hussein, E. M. A., D. A. Meneley, and S. Banerjee. "Single-exposure neutron tomography of two-phase flow." International Journal of Multiphase Flow 12, no. 1 (1986): 1–34. http://dx.doi.org/10.1016/0301-9322(86)90002-9.

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7

Sookprasong, P., J. P. Brill, and Z. Schmidt. "Two-Phase Flow in Piping Components." Journal of Energy Resources Technology 108, no. 3 (1986): 197–201. http://dx.doi.org/10.1115/1.3231264.

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Two-phase and single-phase pressure drop data were obtained for flow in horizontal 5.08-cm-dia pipe and piping components that included: a 9.14-m straight section of pipe; a gate valve; an elbow; a combination of elbow and gate valve separated by different pipe lengths; a globe valve; a swing check valve; and a union. Single-phase pressure drops produced by each component were used to establish the resistance coefficient, K. This resistance was then used to calculate two-phase pressure drops for each component using the Tremblay and Andrews homogeneous flow model. An acceptable agreement was f

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8

van Noorden, T. L., P. A. M. Boomkamp, M. C. Knaap, and T. M. M. Verheggen. "Transient growth in parallel two-phase flow: Analogies and differences with single-phase flow." Physics of Fluids 10, no. 8 (1998): 2099–101. http://dx.doi.org/10.1063/1.869724.

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9

Salhi, A., C. Rey, and J. M. Rosant. "Pressure Drop in Single-Phase and Two-Phase Couette-Poiseuille Flow." Journal of Fluids Engineering 114, no. 1 (1992): 80–84. http://dx.doi.org/10.1115/1.2910004.

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This paper is concerned with axial pressure gradient in single-phase and two-phase flow at low void fraction in a narrow annular space between two concentric cylinders, the inner one rotating. From experimental results, the coupling function (inertial forces/centrifugal forces) is parameterized by Taylor or Rossby numbers for two values of the intercylindrical width (clearance). The results are discussed with regard to different flow regimes and it is shown in particular that transition from the turbulent vorticed regime to the turbulent regime occurs at Ro ≃ 1. The proposed correlation agrees

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10

Zhao, Jiyun, K. J. Tseng, and C. P. Tso. "ICONE19-43024 Effect of the two phase flow models in the nuclear reactor single channel stability analysis." Proceedings of the International Conference on Nuclear Engineering (ICONE) 2011.19 (2011): _ICONE1943. http://dx.doi.org/10.1299/jsmeicone.2011.19._icone1943_9.

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11

Kaminsky, R. D. "Predicting Single-Phase and Two-Phase Non-Newtonian Flow Behavior in Pipes." Journal of Energy Resources Technology 120, no. 1 (1998): 2–7. http://dx.doi.org/10.1115/1.2795006.

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Improved and novel prediction methods are described for single-phase and two-phase flow of non-Newtonian fluids in pipes. Good predictions are achieved for pressure drop, liquid holdup fraction, and two-phase flow regime. The methods are applicable to any visco-inelastic non-Newtonian fluid and include the effect of surface roughness. The methods utilize a reference fluid for which validated models exist. For single-phase flow, the use of Newtonian and power-law reference fluids are illustrated. For two-phase flow, a Newtonian reference fluid is used. Focus is given to shear-thinning fluids. T

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12

Wang, S. K., S. J. Lee, O. C. Jones, and R. T. Lahey. "Statistical Analysis of Turbulent Two-Phase Pipe Flow." Journal of Fluids Engineering 112, no. 1 (1990): 89–95. http://dx.doi.org/10.1115/1.2909374.

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The statistical characteristics of turbulent two-phase pipe flow have been evaluated. In particular, the autocorrelation functions and the power spectral density functions of the axial turbulence fluctuations in the liquid phase were determined. The high frequency content of the power spectrum in bubbly two-phase pipe flow was found to be significantly larger than in single-phase pipe flow and, in agreement with previous studies of homogeneous two-phase flows (Lance et al., 1983), diminished asymptotically with a characteristic −8/3 slope at high frequency. The power spectrum and the autocorre

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13

Nikitopoulos, D. E. "Mach Number Scaling of Single-Component, Two-Phase Flow." Journal of Fluids Engineering 115, no. 4 (1993): 772–77. http://dx.doi.org/10.1115/1.2910211.

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A simple two-fluid formulation is used to investigate compressibility effects and Mach number scaling for equilibrium, evaporating two-phase flow. The definition of the local two-phase Mach number emerges from a critical flow analysis. Comparisons of the theoretical critical mass flux with existing experimental data obtained in steam-water flows show very good agreement for moderate and high qualities over a wide critical pressure range. Within this quality range the predicted critical mass flux is quite insensitive to the velocity ratio. The analysis confirms previous observations, based on h

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14

Hart, J., J. Ellenberger, and P. J. Hamersma. "Single- and two-phase flow through helically coiled tubes." Chemical Engineering Science 43, no. 4 (1988): 775–83. http://dx.doi.org/10.1016/0009-2509(88)80072-1.

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15

Ba, Te, Arthur Teck Bin Lim, and Chang Wei Kang. "Numerical Study of the Single-Phase and Two-Phase Flow in a Centrifugal Pump." Applied Mechanics and Materials 307 (February 2013): 215–18. http://dx.doi.org/10.4028/www.scientific.net/amm.307.215.

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The paper presents the numerical investigation of a radial flow centrifugal pump with 2D curvature blade geometry. The geometry is based on the experimental equipment by Anagostopulos. Single phase (water) flow is modeled with a normal mass flow rate and rotation speed. Pressure distribution and fluid streamlines are evaluated and visualized. An extension of the model to transient flow and two-phase flow simulation has been done to see the effect of impeller rotation and gas entrainment in the centrifugal operation procedure.

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16

NISHIO, SHIGEFUMI. "Single-Phase Laminar-Flow Heat Transfer and Two-Phase Oscillating-Flow Heat Transport in Microchannels." Heat Transfer Engineering 25, no. 3 (2004): 31–43. http://dx.doi.org/10.1080/01457630490280065.

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17

Abedini, Ehsan, Taleb Zarei, Masoud Afrand, and Somchai Wongwises. "Experimental study of transition flow from single phase to two phase flow boiling in nanofluids." Journal of Molecular Liquids 231 (April 2017): 11–19. http://dx.doi.org/10.1016/j.molliq.2017.01.049.

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18

AKIYOSHI, Goki, Mohammad Ariful ISLAM, Akio MIYARA, and Takahisa KUROKAWA. "Flow Behavior of Single and Two-Phase Flow inside Herringbone Microfin Tubes." Proceedings of Conference of Kyushu Branch 2004.57 (2004): 125–26. http://dx.doi.org/10.1299/jsmekyushu.2004.57.125.

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19

Messilem, Abdelkader, Abdelwahid Azzi, Ammar Zeghloul, Faiza Saidj, Hiba Bouyahiaoui, and Al-Sarkhi Abdelsalam. "Single- and two-phase pressure drop through vertical Venturis." Proceedings of the Institution of Mechanical Engineers, Part C: Journal of Mechanical Engineering Science 234, no. 12 (2020): 2349–59. http://dx.doi.org/10.1177/0954406220906424.

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An experimental investigation of the pressure drops measurements in a Venturi placed in a vertical pipe is achieved. Venturis with diameter ratios equal to 0.4, 0.55, and 0.75 were employed. Differential pressure transducers were used to measure the pressure drop between the Venturi inlet and the throat sections. The void fraction was measured upstream the Venturi using a conductance probe technique. Air and water superficial velocities ranges were chosen to cover single-phase flow and bubbly, slug, and churn flow regimes. The single-phase pressure drop increases with the liquid superficial ve

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20

Hegde, Pradeep, K. N. Seetharamu, P. A. Aswatha Narayana, and Zulkifly Abdullah. "Two-Phase Stacked Microchannel Heat Sinks for Microelectronics Cooling." Journal of Microelectronics and Electronic Packaging 2, no. 2 (2005): 122–31. http://dx.doi.org/10.4071/1551-4897-2.2.122.

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Stacked microchannel heat sinks with two-phase flow have been analyzed using the Finite Element Method (FEM). The present method is a simple and practical approach for analyzing the thermal performance of single or multi layered microchannel heat sinks with either single or two-phase flow. A unique 10 noded finite element is used for the channel discretization. Two-phase thermal resistance, pressure drop and pumping power of single, double and triple stack microchannel heat sinks are determined at different base heat fluxes ranging from 150 W/cm2 to 300 W/cm2. The temperature distribution alon

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21

Supa-Amornkul, Savalaxs, Frank R. Steward, and Derek H. Lister. "Modeling Two-Phase Flow in Pipe Bends." Journal of Pressure Vessel Technology 127, no. 2 (2004): 204–9. http://dx.doi.org/10.1115/1.1904063.

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In order to have a better understanding of the interaction between the two-phase steam-water coolant in the outlet feeder pipes of the primary heat transport system of some CANDU reactors and the piping material, themalhydraulic modelling is being performed with a commercial computational fluid dynamics (CFD) code—FLUENT 6.1. The modeling has attempted to describe the results of flow visualization experiments performed in a transparent feeder pipe with air-water mixtures at temperatures below 55°C. The CFD code solves two sets of transport equations—one for each phase. Both phases are first tr

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22

Sharifi, Soheyl, Mohammad Reza Aligoodarz, and Alireza Rahbari. "Thermohydraulic performance of Al2O3-water nanofluid during single-phase flow and two-phase subcooled flow boiling." International Journal of Thermal Sciences 179 (September 2022): 107605. http://dx.doi.org/10.1016/j.ijthermalsci.2022.107605.

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23

Bai, Bofeng, Maolong Liu, Xiaofei Lv, Junjie Yan, Xiao Yan, and Zejun Xiao. "Correlations for predicting single phase and two-phase flow pressure drop in pebble bed flow channels." Nuclear Engineering and Design 241, no. 12 (2011): 4767–74. http://dx.doi.org/10.1016/j.nucengdes.2011.06.025.

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24

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 (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, wh

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25

YEH, LI-MING. "HOMOGENIZATION OF TWO-PHASE FLOW IN FRACTURED MEDIA." Mathematical Models and Methods in Applied Sciences 16, no. 10 (2006): 1627–51. http://dx.doi.org/10.1142/s0218202506001650.

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In a fractured medium, there is an interconnected system of fracture planes dividing the porous rock into a collection of matrix blocks. The fracture planes, while very thin, form paths of high permeability. Most of the fluids reside in matrix blocks, where they move very slow. Let ε denote the size ratio of the matrix blocks to the whole medium and let the width of the fracture planes and the porous block diameter be in the same order. If permeability ratio of matrix blocks to fracture planes is of order ε2, microscopic models for two-phase, incompressible, immiscible flow in fractured media

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26

Fuquan, Song, Song Xingxing, Wang Yong, and Sun Yeheng. "Single- and two-phase flow model in low-permeability reservoir." Petroleum 5, no. 2 (2019): 183–90. http://dx.doi.org/10.1016/j.petlm.2018.05.004.

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27

Wu, Yuanqing, and Shuyu Sun. "Equivalence of two models in single-phase multicomponent flow simulations." Computers & Mathematics with Applications 71, no. 6 (2016): 1303–16. http://dx.doi.org/10.1016/j.camwa.2016.02.008.

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28

Yüncü, H., O. T. Yildirim, and S. Kakaç. "Two-phase flow instabilities in a horizontal single boiling channel." Applied Scientific Research 48, no. 1 (1991): 83–104. http://dx.doi.org/10.1007/bf01998667.

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29

Ranjith, P. G., S. K. Choi, and M. Fourar. "Characterization of two-phase flow in a single rock joint." International Journal of Rock Mechanics and Mining Sciences 43, no. 2 (2006): 216–23. http://dx.doi.org/10.1016/j.ijrmms.2005.06.001.

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30

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 m

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31

Wu, Ke-Jun, Valentina Nappo, and Simon Kuhn. "Hydrodynamic Study of Single- and Two-Phase Flow in an Advanced-Flow Reactor." Industrial & Engineering Chemistry Research 54, no. 30 (2015): 7554–64. http://dx.doi.org/10.1021/acs.iecr.5b01444.

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32

Vasilev, Maksim P., and Rufat Sh Abiev. "Gas–Liquid Two-Phase Flow and Heat Transfer without Phase Change in Microfluidic Heat Exchanger." Fluids 6, no. 4 (2021): 150. http://dx.doi.org/10.3390/fluids6040150.

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This work presents an experimental study of the possibility of intensifying in microfluidic heat exchangers (MFHE) by creating a two-phase segmented flow (gas–liquid). Measurements of convective heat transfer were carried out using an MFHE, consisting of six channels 1 × 1 mm. Experimental studies have shown that segmented flow makes it possible to increase the Nusselt number of a laminar flow in MFHE up to 1.67 and reduce thermal resistance up to 1.7 times compared to single-phase flow. At the same time, it was found that the intensification of heat exchange by a two-phase flow is observed on

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33

Mohamed, Adel Esmaeel, and M. Hussain Hassan Nashaat. "Analysis and comparison of single-phase induction motor operation from single- and two-phase power sources using MATLAB simulation results." International Journal of Power Electronics and Drive Systems (IJPEDS) 13, no. 3 (2022): 1380–89. https://doi.org/10.11591/ijpeds.v13.i3.pp1380-1389.

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Single phase induction motor (SPIM) has zero torque, this motor has many types and the main objective is to find the starting torque of the motor. This is done by providing auxiliary coils that are mechanically separated or weakened after 75% of the engine speed. The real problem here is that these auxiliary windings occupy a third of the iron core of the motor, and when they are separated or weakened, the capacity of the iron core is not fully used and the main windings must withstand the rated load current alone which shortens the life of the motor and reduces the hours of continuous operati

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34

Koukouvinis, P., and M. Gavaises. "Simulation of throttle flow with two phase and single phase homogenous equilibrium model." Journal of Physics: Conference Series 656 (December 3, 2015): 012086. http://dx.doi.org/10.1088/1742-6596/656/1/012086.

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35

Al-Ansary, Hany, and Sheldon Jeter. "Numerical and Experimental Analysis of Single-Phase and Two-Phase Flow in Ejectors." HVAC&R Research 10, no. 4 (2004): 521–38. http://dx.doi.org/10.1080/10789669.2004.10391118.

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36

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 (1998): 229–47. http://dx.doi.org/10.1016/s0950-4230(98)00007-2.

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37

BÉG, O. ANWAR, M. M. RASHIDI, M. AKBARI, and A. HOSSEINI. "COMPARATIVE NUMERICAL STUDY OF SINGLE-PHASE AND TWO-PHASE MODELS FOR BIO-NANOFLUID TRANSPORT PHENOMENA." Journal of Mechanics in Medicine and Biology 14, no. 01 (2014): 1450011. http://dx.doi.org/10.1142/s0219519414500110.

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A computational fluid dynamics (CFD) simulation of laminar convection of Al 2 O 3–water bio-nanofluids in a circular tube under constant wall temperature conditions was conducted, employing a single-phase model and three different two-phase models (volume of fluid (VOF), mixture and Eulerian). The steady-state, three-dimensional flow conservation equations were discretised using the finite volume method (FVM). Several parameters such as temperature, flow field, skin friction and heat transfer coefficient were computed. The computations showed that CFD predictions with the three different two-p

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38

Ruiz Maraggi, L. M., L. W. Lake, and M. P. Walsh. "A Two-Phase Flow Model for Reserves Estimation in Tight-Oil and Gas-Condensate Reservoirs Using Scaling Principles." SPE Reservoir Evaluation & Engineering 25, no. 01 (2021): 81–98. http://dx.doi.org/10.2118/199032-pa.

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Summary A common approach to forecast production from unconventional reservoirs is to extrapolate single-phase flow solutions. This approach ignores the effects of multiphase flow, which exist once the reservoir pressure falls below the bubble/dewpoint. This work introduces a new two-phase (oil and gas) flow solution suitable to extrapolating oil and gas production using scaling principles. In addition, this study compares the application of the two-phase and the single-phase solutions to estimates of production from tight-oil wells in the Wolfcamp Formation of west Texas. First, we combine th

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39

Warren, B. A., and J. F. Klausner. "Developing Lengths in Horizontal Two-Phase Bubbly Flow." Journal of Fluids Engineering 117, no. 3 (1995): 512–18. http://dx.doi.org/10.1115/1.2817292.

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An air-water two-phase flow facility with a 19.1 mm i.d. test section has been fabricated. Local measurements of pressure drop for two-phase horizontal bubbly flow and single-phase flow downstream of various orifices have been obtained over a range of flow conditions. The wall shear stress developing length is obtained from the pressure drop profile. A developing length correlation is presented in which the relative deviation is 6 percent. The fully developed vapor volume fraction has also been measured up- and downstream of the orifice. A simple correlation for vapor volume fraction is presen

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40

Hua, Hong, Xiao Bing Liu, Shun Bing Ou, and Yong Zhong Zeng. "Numerical Simulation of 3D Solid-Liquid Two-Phase Turbulence Flow in Axial-Flow Pump Impeller." Applied Mechanics and Materials 212-213 (October 2012): 1237–43. http://dx.doi.org/10.4028/www.scientific.net/amm.212-213.1237.

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With the use of the RNG k-ε turbulence model and the SIMPLEC algorithm, as well as after the secondary development of the software Fluent, the velocity field and pressure field of a axial flow impeller were numerically simulated in the single-phase (clear water) and the solid-liquid two-phase conditions. The distributions of pressure, velocity and solid concentration in the impeller under the single-phase flow and the solid-liquid two-phase flow conditions were compared. This study has shown that the numerical simulation results are the same as the actual situation.

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41

Yang, Dong, Zhiqin Kang, and Yangsheng Zhao. "Mechanism of the Gas-Liquid Two-Phase Chaotic Flow in Single Fracture." Geofluids 2020 (August 25, 2020): 1–11. http://dx.doi.org/10.1155/2020/8860058.

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The seepage of gas-liquid two-phase flow in fracture is a commonly found phenomenon in nature. To reveal the underlying mechanism and the critical condition of the chaos occurrence, a stochastic gas-liquid two-phase flow seepage model is established, and then investigated through a numerical simulation and a horizontal Hele-Shaw experiment. The numerical simulation and laboratory experiment results show that the seepage chaos of gas-liquid two-phase flow takes place when the relative saturation is in the range of gas relative saturation 44%-70%, and the occurrence probability can be expressed

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42

Tolpadi, A. K. "Calculation of Two-Phase Flow in Gas Turbine Combustors." Journal of Engineering for Gas Turbines and Power 117, no. 4 (1995): 695–703. http://dx.doi.org/10.1115/1.2815455.

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A method is presented for computing steady two-phase turbulent combusting flow in a gas turbine combustor. The gas phase equations are solved in an Eulerian frame of reference. The two-phase calculations are performed by using a liquid droplet spray combustion model and treating the motion of the evaporating fuel droplets in a Lagrangian frame of reference. The numerical algorithm employs nonorthogonal curvilinear coordinates, a multigrid iterative solution procedure, the standard k-ε turbulence model, and a combustion model comprising an assumed shape probability density function and the cons

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43

Nikulin, A., V. Melikhov, and O. Melikhov. "SIMULATION OF SINGLE-PHASE AND TWO-PHASE FLOW THROUGH A SUBMERGED PERFORATED SHEET USING OPENFOAM CODE." Eurasian Journal of Mathematical and Computer Applications 12, no. 4 (2024): 92–104. https://doi.org/10.32523/2306-6172-2024-12-4-92-104.

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The aim of the study is to numerically simulate the flow of steam/steam-water mixture through one periodic cell of a submerged perforated sheet, which is an important element of the separation scheme of a horizontal steam generator. The OpenFOAM code is used as a calculation tool. First, the flow of single-phase steam was considered. A comparison of the values of pressure drops on the perforated sheet obtained using the OpenFOAM code for two turbulence models with pressure drops determined by other CFD code FlowVision, various approximate formulas and experimental data shows that the variation

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44

Song, S. H., Kyosuke Kishida, Masahiko Demura, Myung Hoon Oh, Dang Moon Wee, and Toshiyuki Hirano. "Plane Strain Compression of Single Crystalline Ni₃Al-Base Intermetallic Compounds." Materials Science Forum 495-497 (September 2005): 767–74. http://dx.doi.org/10.4028/www.scientific.net/msf.495-497.767.

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Anisotropic deformation behavior of single crystalline Ni3Al-base intermetallic compounds, including Ni3Al single-phase and Ni/Ni3Al two-phase alloys, was systematically studied by the plane strain compression tests. Plastic flow behavior of single phase Ni3Al is strongly dependent on the initial crystal orientation and the flow stress becomes higher with increasing the numbers of the operative slip planes. In the case of the Ni/Ni3Al two phase alloys, the flow behavior is found to be divided into two stages. Such flow behavior is considered to be closely related to the difference in the defor

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45

Galvis, Elmer, and Richard Culham. "Measurements and flow pattern visualizations of two-phase flow boiling in single channel microevaporators." International Journal of Multiphase Flow 42 (June 2012): 52–61. http://dx.doi.org/10.1016/j.ijmultiphaseflow.2012.01.009.

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46

Du, Xiaoju, and Ole Jørgen Nydal. "Flow models and numerical schemes for single/two-phase transient flow in one dimension." Applied Mathematical Modelling 42 (February 2017): 145–60. http://dx.doi.org/10.1016/j.apm.2016.10.017.

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47

Song, Li Jun, Qian Peng, Xiao Liu, and Wu Hui Chen. "Study on a Uniform Algorithm for Single-Phase and Three-Phase Load Flow Calculation." Advanced Materials Research 614-615 (December 2012): 957–65. http://dx.doi.org/10.4028/www.scientific.net/amr.614-615.957.

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This paper presents a uniform algorithm for single-phase and three-phase load flow calculation. Firstly, two iterative equations with static factors are studied for single-phase power flow calculation based on Gauss power flow algorithm. One is used for all PQ nodes iteration similar to the traditional Gauss power flow algorithm, and the other one is exploited for all PV nodes and the slack node, which is a new algorithm studied in this paper. Then, the three-phase power flow iterative equations are studied. Virtual generator nodes are generated so that it is enough to built equations to solve

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Baroncini, Virgínia, Cicero Martelli, Marco da Silva, and Rigoberto Morales. "Single- and Two-Phase Flow Characterization Using Optical Fiber Bragg Gratings." Sensors 15, no. 3 (2015): 6549–59. http://dx.doi.org/10.3390/s150306549.

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De Salve, M., M. Orio, and B. Panella. "Single and two-phase flow fluid dynamics in parallel helical coils." Journal of Physics: Conference Series 501 (April 10, 2014): 012014. http://dx.doi.org/10.1088/1742-6596/501/1/012014.

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CHIBA, Noriko, Kazuhiro KIKKAWA, Sachiyo HORIKI, and Masahiro OSAKABE. "Discharging Behavior of Single and Two-Phase Flow through Safety Valve." TRANSACTIONS OF THE JAPAN SOCIETY OF MECHANICAL ENGINEERS Series B 78, no. 794 (2012): 1739–48. http://dx.doi.org/10.1299/kikaib.78.1739.

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