Relevant bibliographies by topics / Liquid-liquid flows

Academic literature on the topic 'Liquid-liquid flows'

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Published: 10 December 2022
Last updated: 28 January 2023

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Journal articles on the topic "Liquid-liquid flows"

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Vempati, Bhadraiah, Mahesh V. Panchagnula, Alparslan Öztekin, and Sudhakar Neti. "Numerical Investigation of Liquid-Liquid Coaxial Flows." Journal of Fluids Engineering 129, no. 6 (December 8, 2006): 713–19. http://dx.doi.org/10.1115/1.2734223.

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This paper presents numerical results of the interfacial dynamics of axisymmetric liquid-liquid flows when the denser liquid is injected with a parabolic inlet velocity profile into a coflowing lighter fluid. The flow dynamics are studied as a function of the individual phase Reynolds numbers, viscosity ratio, velocity ratio, Bond number, and capillary number. Unsteady, axisymmetric flows of two immiscible fluids have been studied using commercial software, FLUENT® with the combination of volume of fluid (VOF) and continuous surface force (CSF) methods. The flows have been categorized as “flow-accelerated regime (FAR) and “flow-decelerated regime” (FDR) based on acceleration/deceleration of the injected fluid. The injected jet diameter decreases when the average inlet velocity ratio is less than unity. The outer fluid velocity has a significant effect on the shape and evolution of the jet as it progresses downstream. As the outer liquid flow rate is increased, the intact jet length is stretched to longer lengths while the jet radius is reduced due to interfacial stresses. The jet radius appears to increase with increasing viscosity ratio and ratio of Bond and capillary numbers. The results of numerical simulations using FLUENT agree well with experimental measurements and the far-field self-similar solution.
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Angeli, P., and G. F. Hewitt. "Pressure gradient in horizontal liquid–liquid flows." International Journal of Multiphase Flow 24, no. 7 (November 1999): 1183–203. http://dx.doi.org/10.1016/s0301-9322(98)00006-8.

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Ioannou, Karolina, Ole Jorgen Nydal, and Panagiota Angeli. "Phase inversion in dispersed liquid–liquid flows." Experimental Thermal and Fluid Science 29, no. 3 (March 2005): 331–39. http://dx.doi.org/10.1016/j.expthermflusci.2004.05.003.

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Vigneaux, P., P. Chenais, and J. P. Hulin. "Liquid-liquid flows in an inclined pipe." AIChE Journal 34, no. 5 (May 1988): 781–89. http://dx.doi.org/10.1002/aic.690340508.

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SOTOWA, Ken-Ichiro. "Gas-Liquid and Liquid-Liquid Multiphase Flows and Microreaction Technology." JAPANESE JOURNAL OF MULTIPHASE FLOW 27, no. 3 (2013): 258–65. http://dx.doi.org/10.3811/jjmf.27.258.

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Hewitt, Geoffrey, C. P. Hale, B. Hu, W. L. Wong, and S. M. Richardson. "GAMMAS AND X-RAY TOMOGRAPHY OF LIQUID-LIQUID AND GAS-LIQUID-LIQUID FLOWS." Multiphase Science and Technology 19, no. 3 (2007): 241–67. http://dx.doi.org/10.1615/multscientechn.v19.i3.30.

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Durst, F., B. Schönung, K. Selanger, and M. Winter. "Bubble-driven liquid flows." Journal of Fluid Mechanics 170 (September 1986): 53–82. http://dx.doi.org/10.1017/s0022112086000800.

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Detailed information is provided in this paper on the physics of momentum transfer in bubble-driven liquid flows. Experimental information is obtained on the flow around bubbles and on the axisymmetric bubble-driven liquid flow inside liquid-filled cylinders located with their axes in the vertical direction. A laser-Doppler anemometer extended for particulate two-phase flows is employed for these measurements to yield local fluid velocity information as well as the rise velocity of bubbles. The bubble top radius and the bubble shape were also found from these measurements.Utilizing experimentally gained information and employing the basic equations for particulate two-phase flows, permits finite difference equations to be formulated that allow bubble-driven liquid flows to be computed. Results are presented for boundary conditions corresponding to those of the experimental studies. Comparisons of numerical and experimental results are shown to be in good agreement. This is taken as a justification to employ the developed computer programs to carry out parameter studies for bubble-driven liquid flow inside circular cylinders. Results of these studies are presented and discussed.
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Richardson, S. M. "Choking of liquid flows." Journal of Fluid Mechanics 199 (February 1989): 563–68. http://dx.doi.org/10.1017/s0022112089000480.

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It is well-known that laminar flow of a liquid in a duct is predicted to choke if the viscosity of the liquid increases exponentially with increasing pressure. In other words, the pressure drop in the duct is predicted to become unbounded when the volumetric flow rate reaches a critical finite value. Choking is not observed in practice, however: the reason why is investigated here. It is shown that choking is always predicted to occur if the viscosity is independent of temperature or heat generation by viscous dissipation is neglected. If the viscosity decreases exponentially with increasing temperature and heat generation is not neglected, however, and if the temperature field is fully developed or if the flow is adiabatic, it is shown that choking is predicted not to occur.
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Raj, Richa, Nikita Mathur, and Vivek V. Buwa. "Numerical Simulations of Liquid−Liquid Flows in Microchannels." Industrial & Engineering Chemistry Research 49, no. 21 (November 3, 2010): 10606–14. http://dx.doi.org/10.1021/ie100626a.

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Shi, Jing, and Hoi Yeung. "Characterization of liquid-liquid flows in horizontal pipes." AIChE Journal 63, no. 3 (August 26, 2016): 1132–43. http://dx.doi.org/10.1002/aic.15452.

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Dissertations / Theses on the topic "Liquid-liquid flows"

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Hasan, Norpa'iza Mohamad. "Stratifying liquid-liquid flows." Thesis, University of Nottingham, 2006. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.440994.

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Simmons, Mark John Harry. "Liquid-liquid flows and separation." Thesis, University of Nottingham, 1998. http://eprints.nottingham.ac.uk/27793/.

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The transport and separation of oil and water is a vital process to the oil and chemical industries. Fluids exiting from oil wells usually consist of gas, oil and water and these three phases need to be transported and separated before they can be processed further. Operation of the primary separators has often proved to be problematic due to the change in composition of the fluids as the well matures, often accompanied by the build up of sand or asphaltenes. These vessels are very expensive to install so there is motivation to improve their design and performance. One major factor affecting separator performance is the phase distribution of the inlet flow, as reflected in the flow pattern and droplet size. In this work, flow pattern boundaries and drop sizes of liquid-liquid dispersions were measured for vertical and horizontal flow of a kerosene and water mixture in a 0.063m tube. Drop size was investigated by using two different laser optical techniques. A laser backscatter technique was employed for concentrated dispersions and a diffraction technique was used at low concentrations. In order to develop a greater understanding of separator performance, a 1/5th-scale model was constructed of diameter 0.6m and length 205m. Residence Time Distributions were obtained for a range of different internal configurations and flow rates using a colorimetric tracer technique. Flow rates of 1.5-4 kg/s oil and 1-4 kg/s water were used and the vessel was equipped with a perforated flow-spreading baffle at the inlet and an overflow weir. Experiments were performed with no internals and with dip or side baffles. The side baffles acted to create quiescent zones within the vessel while the dip baffle caused a local acceleration of both phases. These situations are similar to those that can be caused by blocked internals or existing baffling or structured packing within field separators. A Residence Time Distribution model of a primary separator, the Alternative Path Model, was developed using transfer functions. This model has the ability to reproduce features of the experimental data by representing the flow as a series of continuous stirred tanks in series or in parallel. The model was used to develop parameters that could be used to obtain information about the performance of the separator. This model was also applied to Residence Time Distribution data obtained from field separators by BP Exploration, to relate features of the pilot scale separator to the field vessels.
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Angeli, Panagiota. "Liquid-liquid dispersed flows in horizontal pipes." Thesis, Boston Spa, U.K. : British Library Document Supply Centre, 1996. http://ethos.bl.uk/OrderDetails.do?did=1&uin=uk.bl.ethos.321543.

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Liu, Lan. "Optical and computational studies of liquid-liquid flows." Thesis, Imperial College London, 2005. http://hdl.handle.net/10044/1/7937.

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Hussain, Siti Aslina. "Experimental and computational studies of liquid-liquid dispersed flows." Thesis, Imperial College London, 2004. http://hdl.handle.net/10044/1/7998.

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Yusoff, Nazrul Hizam. "Stratifying of liquid-liquid two phase flows through sudden expansion." Thesis, University of Nottingham, 2012. http://eprints.nottingham.ac.uk/12939/.

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The transport and separation of oil and water is an essential process to the oil and chemical industries. Although transporting the mixtures is often necessary due to few reasons, it is generally beneficial to separate out the phases in order to reduce installation and maintenance costs, at the same time, avoiding safety problems. Thus, separation of liquid-liquid flows is a necessary part of many industrial processes. Hence, knowledge of two-phase flow dynamics is important for the design optimisation of separators. Therefore, the aim of this research is to investigate the feasibility of a sudden pipe expansion to be used as phase separator because it compact in design and capable for converting dispersed flow to stratified flow. In the test section, spatial distribution of the liquid-liquid phases in a dynamics flow system was visualised for the first time for by means of capacitance Wire Mesh Sensor (CapWMS), providing instantaneous information about the interface shapes, waves and phase layer evolution of oil-water flow. Visual assessment and analysis of the WMS data showed three distinct layers: an oil layer at the pipe top; a water layer at the pipe bottom and a mixed layer between them. The interfaces that form between the separated phases (oil or water) and the mixed layer were classified as oil interface or water interface. Results showed interface shapes were initially concave or convex near to the inlet of the test section and became flat further downstream the expansion, especially for water interfaces. There were no waves observed for horizontal and downward pipe orientations at all flow conditions and axial position downstream of the expansion. As for the upward inclined pipe orientation, waves were found, and they formed at position close to the inlet at all input oil volume fraction except at 0.2 OVF. The amplitude of the waves was: ~ 0.29D for 0.8 OVF; ~ 0.22D for 0.6 OVF and ~ 0.26D for 0.4 OVF. The higher the input oil volume fraction, the larger the waves become. In conclusion, the WMS results demonstrated that spatial distributions are strongly dependent on the mixture velocity, input oil fraction and inclination angles for the far position. In this present work, droplets were found to be larger near the interface. Drops were large nearer to the interface at the near position (10D) for all pipe orientations and throughout the test section for horizontal flow. The drops size decreased when the distance from the interface increased for these pipe configurations. As for the furthest position from the expansion for upward and downward inclined pipe orientation, larger droplets could also be seen at distance away from the interface and vice versa. The gravity or buoyant force is one of the contributing factors to the settling of the droplets. These forces are acting simultaneously on the droplets i.e. if the buoyant force which tends to spread the droplets throughout the pipe cross-section, is not large enough to overcome the settling tendency of gravity settling of the droplets occurs. Hence, the droplets that are non-uniformly scattered within the continuous phase begin to coalesce as they flow further downstream the pipe, producing larger drops. In addition, as the distance from expansion increased, the mixed layer becomes narrow and more drops begin to coalescence to form large drop due to increased droplet-droplet collision. Owing to these factors, results indicate that the mechanisms of coalescence occurred faster at the bottom, for water droplets and at the top, for oil droplets than the other locations in a pipe cross-section. For a better separation design, the coalescence process should occur at the aforementioned (bottom for water and top for oil) locations within the expansion pipe. However, at higher mixture velocities the mixed layer would be responsible for the smaller droplet size for horizontal and both inclinations of pipe orientation. The mixed layer dominated almost entirely in the pipe cross-section.
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Costigan, G. "Flow pattern transitions in vertical gas - liquid flows." Thesis, University of Oxford, 1997. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.361925.

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Yang, Limin. "Liquid-liquid two-phase flows at T-junctions and through expansions." Thesis, University of Nottingham, 2003. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.404047.

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Morgan, Rhys Gareth. "Studies of liquid-liquid two-phase flows using laser-based methods." Thesis, Imperial College London, 2012. http://hdl.handle.net/10044/1/10145.

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The research described in this thesis has been focused on the detailed investigation of horizontal co-current liquid-liquid two-phase flows. The experiments were carried out in channels of square and circular cross section and involved the use of two immiscible liquids of matched refractive index; namely an oil (Exxol™D80) and a 81.7 wt% glycerol-water solution. The experiments were carried out in a refurbished liquid-liquid flow facility (TOWER) and the focus was on examining the flows using high-speed laser-based visualisation methods which allowed both qualitative evaluation of the nature of the flows (i.e. the flow patterns) and quantitative measurements of parameters such as drop size and velocity distribution. The laser-based techniques used included Planar Laser Induced Fluorescence (PLIF), Particle Tracking Velocimetry (PTV) and Particle Image Velocimetry (PIV). Using these techniques, it was possible to obtain high spatial and temporal resolution measurements of velocity and phase distribution of liquid-liquid flows which enabled the detailed diagnostic inspection to an extent that has not been previously possible. 144 experiments were carried out in three experimental campaigns. In the first campaign, a square cross section channel was used in order to avoid image distortion by the channel walls. In the second and third campaigns, a circular tube was employed and a graticule correction method was used to correct the distortion to the PLIF and PTV/PIV images which occurs when the circular cross-section visualisation cell is used. In the two circular tube experiments, two methods of injection of the phases were used: (1) the heavier (glycerol solution) phase was injected in its natural location at the bottom of the channel, and (2) in the second case the heavier phase was injected at the top of the channel. The PLIF images gave a clear indication of the distribution of the phases at the channel centre line and have been used qualitatively in obtaining information about the flow patterns occurring. The PLIF images have also been used quantitatively in generating data on phase distribution, insitu phase fraction, interface level and drop size distribution. Much of the data on in-situ phase fraction and interface level fits well with a simple laminar-laminar stratified flow model. The PTV/PIV method provided extensive data on velocity profiles; in the lower (aqueous glycerol solution) phase, the profile usually showed the curved shape characteristic of laminar flow and in the upper (Exxol™D80) phase, the velocity profile often showed the flattened form characteristic of turbulent flow.
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Badeau, Allen E. "A droplet formation and entrainment model for stratified liquid-liquid flows." Morgantown, W. Va. : [West Virginia University Libraries], 2000. http://etd.wvu.edu/templates/showETD.cfm?recnum=1737.

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Thesis (M.S.)--West Virginia University, 2000.
Title from document title page. Document formatted into pages; contains xiii, 150 p. : ill. (some col.). Includes abstract. Includes bibliographical references (p. 140-144).
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Books on the topic "Liquid-liquid flows"

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Azzopardi, B. J. Gas-liquid flows. New York, NY: Begell House, 2005.

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Azzopardi, B. J. Gas-liquid flows. New York: Begell House, 2006.

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American Society of Mechanical Engineers. Winter Meeting. Fundamentals of gas-liquid flows. New York: American Society of Mechanical Engineers, 1988.

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1931-, Branover Herman, Mond Michael, and Unger Yeshajahu, eds. Liquid-metal flows: Magnetohydrodynamics and applications. Washington, DC: American Institute of Aeronautics and Astronautics, 1988.

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Savino, Raffaele. Surface tension-driven flows and applications, 2006. Kerala, India: Research Signpost, 2006.

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International Symposium on Liquid-Solid Flows. (3rd 1988 Chicago, Ill.). Third international symposium on liquid-solid flows. New York: American Society of Mechanical Engineers, 1988.

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Tryggvason, Gretar. Direct numerical simulations of gas-liquid multiphase flows. Cambridge: Cambridge University Press, 2011.

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A, Galwey, ed. Liquid and vapor flows in porous bodies: Surface phenomena. Amsterdam: Gordon & Breach, 1999.

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Churaev, N. V. Liquid and vapor flows in porous bodies: Surface phenomena. Amsterdam, The Netherlands: Gordon & Breach Science Publishers, 2000.

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Donnelly, Russell J., ed. High Reynolds Number Flows Using Liquid and Gaseous Helium. New York, NY: Springer New York, 1991. http://dx.doi.org/10.1007/978-1-4612-3108-0.

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Book chapters on the topic "Liquid-liquid flows"

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Podgórska, Wioletta. "Fluid–Fluid Dispersions: Liquid–Liquid and Gas–Liquid Systems." In Multiphase Particulate Systems in Turbulent Flows, 221–355. First edition. | New York, NY : CRC Press, Taylor & Francis Group, 2020.: CRC Press, 2019. http://dx.doi.org/10.1201/9781315118383-6.

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Shcherbinin, Ed V. "Electrically Induced Vortical Flows." In Liquid Metal Magnetohydrodynamics, 169–78. Dordrecht: Springer Netherlands, 1989. http://dx.doi.org/10.1007/978-94-009-0999-1_21.

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Podgórska, Wioletta. "Solid–Liquid Systems." In Multiphase Particulate Systems in Turbulent Flows, 357–433. First edition. | New York, NY : CRC Press, Taylor & Francis Group, 2020.: CRC Press, 2019. http://dx.doi.org/10.1201/9781315118383-7.

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Pearson, J. R. A. "Turbulent Gas-Liquid Flows." In Progress and Trends in Rheology V, 45–48. Heidelberg: Steinkopff, 1998. http://dx.doi.org/10.1007/978-3-642-51062-5_14.

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Joo, S. W., S. H. Davis, and S. G. Bankoff. "Instabilities in Evaporating Liquid Films." In Instabilities in Multiphase Flows, 219–29. Boston, MA: Springer US, 1993. http://dx.doi.org/10.1007/978-1-4899-1594-8_18.

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Gerbeth, G., and D. Hamann. "Dispersion of Small Particles in MHD Flows." In Liquid Metal Magnetohydrodynamics, 97–102. Dordrecht: Springer Netherlands, 1989. http://dx.doi.org/10.1007/978-94-009-0999-1_12.

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Fautrelle, Yves. "Fluid Flows Induced by Alternating Magnetic Fields." In Liquid Metal Magnetohydrodynamics, 223–32. Dordrecht: Springer Netherlands, 1989. http://dx.doi.org/10.1007/978-94-009-0999-1_27.

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Lavrent’ev, I. V. "MHD-Flows at High Rm, N and Ha." In Liquid Metal Magnetohydrodynamics, 21–27. Dordrecht: Springer Netherlands, 1989. http://dx.doi.org/10.1007/978-94-009-0999-1_3.

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Christodoulou, Kostas N., Stephan F. Kistler, and P. Randall Schunk. "Advances in Computational Methods for Free-Surface Flows." In Liquid Film Coating, 297–366. Dordrecht: Springer Netherlands, 1997. http://dx.doi.org/10.1007/978-94-011-5342-3_9.

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Naterer, Greg F. "Gas–Liquid Two-Phase Flows." In Advanced Heat Transfer, 207–60. 3rd ed. Boca Raton: CRC Press, 2021. http://dx.doi.org/10.1201/9781003206125-5.

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Conference papers on the topic "Liquid-liquid flows"

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Vempati, Bhadraiah, Mahesh V. Panchagnula, Alparslan O¨ztekin, and Sudhakar Neti. "Numerical Investigation of Liquid-Liquid Coaxial Flows." In ASME 2005 International Mechanical Engineering Congress and Exposition. ASMEDC, 2005. http://dx.doi.org/10.1115/imece2005-80085.

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This paper presents numerical results of the interfacial dynamics of axisymmetric liquid-liquid flows when the more dense liquid is injected in with parabolic inlet velocity profile. The flow dynamics are studied as a function of the individual phase Reynolds numbers, viscosity ratio, velocity ratio, Bond number, and Capillary number. The flows have been categorized as “necking” and “swelling” based on whether the injected fluid radius is smaller or larger than the injection port radius. The jet has been observed to neck when the average inlet velocity ratio is less than unity. The outer fluid velocity has a significant effect on the shape and evolution of the jet as it progresses downstream. As the outer liquid flow rate is increased, the intact jet length is stretched to longer lengths while the jet radius is reduced due to interfacial stresses. The jet radius appears to increase with increase in Bond number and viscosity ratio while it is nearly invariant with changes in Capillary number. The results of numerical simulations using FLUENT® agree well with the results of experimental measurements and the results of self-similar solution.
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Siginer, Dennis A., Li Yunling, and Thomas E. Jacks. "MARANGONI AND BUOYANCY DRIVEN FLOWS OF NON-NEWTONIAN FLUIDS IN LAYERED FLUID SYSTEMS." In International Symposium on Liquid-Liquid Two Phase Flow and Transport Phenomena. Connecticut: Begellhouse, 1997. http://dx.doi.org/10.1615/ichmt.1997.intsymliqtwophaseflowtranspphen.170.

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Kim, Namwon, Michael C. Murphy, Steven A. Soper, and Dimitris E. Nikitopoulos. "Liquid-Liquid Segmented Flows in Polymer Microfluidic Channels." In ASME 2009 7th International Conference on Nanochannels, Microchannels, and Minichannels. ASMEDC, 2009. http://dx.doi.org/10.1115/icnmm2009-82277.

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Liquid-liquid segmented flows in microchannels fabricated on polymer test chips were investigated experimentally. Polymer test chips were prepared using hot embossing of polycarbonate (PC) sheets with micro-milled brass mold inserts. Three different configurations of microchannels were prepared with injection to test channels expansion ratios of 16, 4 and 2 and a fixed test channel geometry. Deionized water with blue food-coloring dye (1% v/v) was used as a dispersed fluid at flow rates (QD) between 0.5 and 60 μl/min. The carrier fluid was perfluorocarbon (FC 3283) with nonionic fluorous-soluble surfactant (Perfluorooctanol, 10% v/v) at flow rates (QC) between 3 and 25 μl/min. The two fluids were injected separately into the chips. Droplet and Plug flows with transient Irregular Segmented flows between two flow regimes were mainly observed in the test channels of the three different chips. Flow pattern maps and transitions between flow regimes were determined in terms of a fixed homogeneous carrier fluid volumetric flow ratio (βC) to compare the effect of the expansion ratios from the injection to the test channels. The droplet and plug regimes were shifted to higher carrier and lower dispersed fluid superficial velocities and the plug flow regime was broader with the lower expansion ratio channels. The transient irregular segmented flow was favored in the higher expansion channel ratio and the interval of transient irregular segmented flow between droplet and plug flow regimes were shorter for the low expansion channel ratios. This is evidence that flow regime maps in micro-channels are not universal and depend on the configuration part of the micro-injection system. The length of the dispersed segmented flows and the distance between consecutive droplets or plugs as a function of βC were determined by image processing of frames acquired via CCD camera with bright field illumination. The average length of the dispersed fluid was shown to scale approximately with βC to the −1.2 power. Velocities of the dispersed droplet and plug flows were measured using double-pulsed laser illumination and were found to be 1.25 ± 0.049 and 1.46 ± 0.077 times faster than the superficial velocity of the segmented flow respectively. Two-phase pressure drop measurements were also carried out for all flow regimes and associated trends were correlated with changes in flow topology. Comparisons of experimental pressure drop with the predictions for a modified Lockhart-Martinelli correlation were also made.
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Adane, Kofi Freeman K., Syed Imran A. Shah, and R. Sean Sanders. "Numerical Study of Liquid-Liquid Vertical Dispersed Flows." In ASME 2012 Fluids Engineering Division Summer Meeting collocated with the ASME 2012 Heat Transfer Summer Conference and the ASME 2012 10th International Conference on Nanochannels, Microchannels, and Minichannels. American Society of Mechanical Engineers, 2012. http://dx.doi.org/10.1115/fedsm2012-72377.

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Numerical simulations of liquid-liquid dispersed flow in a vertical pipe (38mm) have been carried out using the two-fluid approach implemented in a commercial CFD code, ANSYS CFX. A dispersion of oil in water (where water is the continuous phase) was studied. Both fluids were considered as turbulent flows. The k-ε model was used for the continuous phase, with the eddy viscosity of the dispersed phase estimated from that of the continuous phase. A comparison of the present numerical results with previous experimental and numerical results in terms of volume fraction, mean velocity and turbulent kinetic energy is discussed. In general, good agreement between the simulation results and experimental measurements was observed.
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Benzemel, Hafid, Jean-Michel Rosant, and Jack Legrand. "Liquid-Liquid and Gas-Liquid Flow Patterns in a Torus Reactor." In ASME 1998 International Mechanical Engineering Congress and Exposition. American Society of Mechanical Engineers, 1998. http://dx.doi.org/10.1115/imece1998-0764.

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Abstract Two-phase liquid/liquid and gas/liquid flows in a circular torus reactor have been experimentally studied. The goal was to determine the flow structure inside the torus for various volume ratios of the two phases and various circulation velocities. The observed flow patterns are either stratified, dispersed or mixed flows. For the lower rotational speeds, stratified flow is obtained. For the higher speeds, one phase is dispersed within the other, corresponds to the dispersed flow regime. For the moderate speeds, both stratified and dispersed flows coexist in the torus reactor; this defines the mixed flow regime.
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Lamadie, Fabrice, and Laurent Bruel. "In-Line Digital Holographic Measurement for Liquid-Liquid Flows." In ASME 2013 Fluids Engineering Division Summer Meeting. ASME, 2013. http://dx.doi.org/10.1115/fedsm2013-16086.

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Habchi, Charbel, Sofiane Ouarets, Thierry Lemenand, Dominique Della-Valle, Jerome Bellettre, and Hassan Peerhossaini. "VISCOSITY EFFECTS ON LIQUID-LIQUID DISPERSION IN LAMINAR FLOWS." In CONV-09. Proceedings of International Symposium on Convective Heat and Mass Transfer in Sustainable Energy. Connecticut: Begellhouse, 2009. http://dx.doi.org/10.1615/ichmt.2009.conv.1280.

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Simmons, M. J. H., Sohail H. Zaidi, and B. J. Azzopardi. "Investigation of liquid/liquid flows using laser-based optical systems." In Optical Science, Engineering and Instrumentation '97, edited by Soyoung S. Cha, James D. Trolinger, and Masaaki Kawahashi. SPIE, 1997. http://dx.doi.org/10.1117/12.293406.

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Schimith Berghe, Lara, Bruno da Silva Fonseca, Priscilla Varges, Monica Naccache, Paulo Roberto de Souza Mendes, Marcia Cristina Khalil de Oliveira, Rafaella Magliano Balbi de Faria, Rogerio Mesquita de Carvalho, and Aline Novaes. "LIQUID-LIQUID DISPLACEMENT FLOWS IN A RADIAL HELE-SHAW CELL." In 19th Brazilian Congress of Thermal Sciences and Engineering. ABCM, 2022. http://dx.doi.org/10.26678/abcm.encit2022.cit22-0244.

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de Souza Mendes, Paulo R., Jane Celnik, Flavio H. Marchesini, Albert Co, Gary L. Leal, Ralph H. Colby, and A. Jeffrey Giacomin. "Liquid-Liquid Displacement Flows in an Annular Space Including Viscoplastic Effects." In THE XV INTERNATIONAL CONGRESS ON RHEOLOGY: The Society of Rheology 80th Annual Meeting. AIP, 2008. http://dx.doi.org/10.1063/1.2964581.

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Reports on the topic "Liquid-liquid flows"

1

McCready, M. J. Evolution of flow disturbances in cocurrent gas-liquid flows. Office of Scientific and Technical Information (OSTI), October 1992. http://dx.doi.org/10.2172/6672200.

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Ellen K. Longmire and John S. Lowengrub. Pinch off and reconnection in liquid/liquid flows: joint experimental and numerical studies. Office of Scientific and Technical Information (OSTI), September 2005. http://dx.doi.org/10.2172/850315.

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Aleksandrova, S., S. Molokov, and C. B. Reed. Modeling of liquid metal duct and free-surface flows using CFX. Office of Scientific and Technical Information (OSTI), July 2002. http://dx.doi.org/10.2172/803913.

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Bechtel, Stephen E. Fluid Mechanics and Rheology of Liquid Fiber Flows: Fundamental Science and Technology Applications. Fort Belvoir, VA: Defense Technical Information Center, October 1998. http://dx.doi.org/10.21236/ada361042.

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Liu, D. D. S., D. J. Patmore, and J. J. Lipsett. Hydrodynamic behaviour of gas-liquid two-phase flows at elevated temperatures and pressures. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1985. http://dx.doi.org/10.4095/302590.

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Hua, T. Q., J. S. Walker, B. F. Picologlou, and C. B. Reed. Three-dimensional MHD (magnetohydrodynamic) flows in rectangular ducts of liquid-metal-cooled blankets. Office of Scientific and Technical Information (OSTI), July 1988. http://dx.doi.org/10.2172/6789158.

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McCready, M. J. Evolution of flow disturbances in cocurrent gas-liquid flows. Final report, November 1, 1993--October 31, 1994. Office of Scientific and Technical Information (OSTI), December 1994. http://dx.doi.org/10.2172/35270.

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McCready, M. J. Evolution of flow disturbances in cocurrent gas-liquid flows. Progress report, November 1, 1992--October 31, 1992. Office of Scientific and Technical Information (OSTI), October 1992. http://dx.doi.org/10.2172/10134227.

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Drake, J. B. Modeling convective Marangoni flows with void movement in the presence of solid-liquid phase change. Office of Scientific and Technical Information (OSTI), January 1990. http://dx.doi.org/10.2172/7273969.

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Morley, Neil B. Numerical and experimental modeling of liquid metal thin film flows in a quasi-coplanar magentic field. Office of Scientific and Technical Information (OSTI), January 1994. http://dx.doi.org/10.2172/467130.

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