Gotowe bibliografie tematyczne / Hydrodynamics- Liquid flow

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  1. Artykuły w czasopismach
  2. Rozprawy doktorskie
  3. Książki
  4. Części książek
  5. Streszczenia konferencji
  6. Raporty organizacyjne

Gotowa bibliografia na temat „Hydrodynamics- Liquid flow”

Autor: Grafiati
Data publikacji: 6 września 2023

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Artykuły w czasopismach na temat "Hydrodynamics- Liquid flow"

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Tojimatovich, Karimov Ikromali, and Rakhmanov Abdukhalim Toshpulat Ugli. "HYDRODYNAMICS OF HEAVY LIQUIDS IN A BUBBLING EXTRACTOR." International Journal of Advance Scientific Research 03, no. 06 (2022): 91–99. http://dx.doi.org/10.37547/ijasr-02-06-13.

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The article proposes a formula for calculating the flow rate of a heavy liquid supplied to the mixing zones of the apparatus. The experimental setup presents the results and analysis of experimental studies carried out to determine the flow rate of heavy liquid in the mixing zone of the bubbling extractor. The analysis confirmed the accuracy of the theoretical equation proposed for calculating the heavy liquid flow rate. According to the results of the study, it was possible to determine the flow rate of heavy liquid depending on the size and coefficient of resistance of the holes.
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Gupta, Raghvendra, Sharon S. Y. Leung, Rogerio Manica, David F. Fletcher, and Brian S. Haynes. "Hydrodynamics of liquid–liquid Taylor flow in microchannels." Chemical Engineering Science 92 (April 2013): 180–89. http://dx.doi.org/10.1016/j.ces.2013.01.013.

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Jovanović, Jovan, Wenya Zhou, Evgeny V. Rebrov, T. A. Nijhuis, Volker Hessel, and Jaap C. Schouten. "Liquid–liquid slug flow: Hydrodynamics and pressure drop." Chemical Engineering Science 66, no. 1 (2011): 42–54. http://dx.doi.org/10.1016/j.ces.2010.09.040.

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Lin, Fanghua, and Changyou Wang. "Recent developments of analysis for hydrodynamic flow of nematic liquid crystals." Philosophical Transactions of the Royal Society A: Mathematical, Physical and Engineering Sciences 372, no. 2029 (2014): 20130361. http://dx.doi.org/10.1098/rsta.2013.0361.

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The study of hydrodynamics of liquid crystals leads to many fascinating mathematical problems, which has prompted various interesting works recently. This article reviews the static Oseen–Frank theory and surveys some recent progress on the existence, regularity, uniqueness and large time asymptotic of the hydrodynamic flow of nematic liquid crystals. We will also propose a few interesting questions for future investigations.
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Wang, Yi. "CFD Simulation on Hydrodynamics of Liquid-Liquid Slug Flow in Microchannel." Advanced Materials Research 936 (June 2014): 1662–65. http://dx.doi.org/10.4028/www.scientific.net/amr.936.1662.

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Hydrodynamics in a liquid-liquid slug flow in a T-junction microchannel of 600μm diameter, operated under a squeezing regime, was simulated with the computational fluid dynamics method. The slug flow generation simulated shows very good agreement with experimental snapshots where the clear slug formation takes place in the vicinity of the T-junction. The internal circulation within each slug was also obtained, which could make us better understand the hydrodynamics of liquid-liquid slug flow in microchannel.
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Nieves-Remacha, María José, Amol A. Kulkarni, and Klavs F. Jensen. "Hydrodynamics of Liquid–Liquid Dispersion in an Advanced-Flow Reactor." Industrial & Engineering Chemistry Research 51, no. 50 (2012): 16251–62. http://dx.doi.org/10.1021/ie301821k.

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Kashid, M. N., D. Fernández Rivas, D. W. Agar, and S. Turek. "On the hydrodynamics of liquid-liquid slug flow capillary microreactors." Asia-Pacific Journal of Chemical Engineering 3, no. 2 (2008): 151–60. http://dx.doi.org/10.1002/apj.127.

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Conan, C., O. Masbernat, S. Décarre, and A. Liné. "Local hydrodynamics in a dispersed-stratified liquid–liquid pipe flow." AIChE Journal 53, no. 11 (2007): 2754–68. http://dx.doi.org/10.1002/aic.11309.

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Zhuang, Tieshuan, Jun Wu, Tao Zhang, and Xiangwei Dong. "A weakly compressible smoothed particle hydrodynamics framework for melting multiphase flow." AIP Advances 12, no. 2 (2022): 025329. http://dx.doi.org/10.1063/5.0057583.

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In this study, the transient process of solid–liquid phase change is modeled and simulated by the multiphase smoothed particle hydrodynamics (SPH) method. First, to simulate the interfacial behaviors of melt liquids, the multiphase SPH model is established for immiscible viscous fluids with a large density ratio, where the environmental liquid surrounding the solid phase is considered, and the surface tension of the melt liquid can be accurately modeled by the continuum surface force method. Based on the multiphase model, the thermal dynamics model is incorporated to describe the heat conducti
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Dijk, P. E., A. M. C. Janse, J. A. M. Kuipers, and W. P. M. van Swaaij. "Hydrodynamics of liquid flow in a rotating cone." International Journal of Numerical Methods for Heat & Fluid Flow 11, no. 5 (2001): 386–412. http://dx.doi.org/10.1108/09615530110397334.

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Rozprawy doktorskie na temat "Hydrodynamics- Liquid flow"

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Abadie, Thomas. "Hydrodynamics of gas-liquid Taylor flow in microchannels." Phd thesis, Toulouse, INPT, 2013. http://oatao.univ-toulouse.fr/11986/1/abadie.pdf.

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This thesis focuses on the hydrodynamics of gas-liquid Taylor flow (or slug flow) in microchannels. These flows, which are generally dominated by surface tension forces, have been investigated in rectangular channels of various cross-sectional aspect ratios by means of both experimental visualizations and numerical simulations. The first experimental part aims at characterizing the bubble generation process (bubble length and frequency of break-up) depending on the operating conditions, the fluid properties, as well as the junction where both fluids merge. Numerical simulations of fully develo
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Welsh, Susan A. "Hydrodynamic characteristics of countercurrent gas-pseudoplastic liquid two-phase channel flow." Thesis, Georgia Institute of Technology, 1998. http://hdl.handle.net/1853/16923.

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Van, der Merwe Werner. "The Morphology of Trickle Flow Liquid Holdup." Diss., University of Pretoria, 2005. http://hdl.handle.net/2263/31385.

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Gravity driven trickle flow of a liquid over a fixed bed in the presence of a gaseous phase is widely encountered throughout the process industry. It is one of the most common ways of contacting multi-phase fluids for reaction or mass transfer purposes. The presence of three phases greatly complicates the mathematical modelling of trickle-bed reactors and makes a description from first principles difficult. Trickle flow performance is usually characterized in terms of hydrodynamic parameters. One such parameter is the liquid holdup. The value and morphology (shape or texture) of the holdup inf
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Stoodley, Paul. "The influence of liquid flow and nutrients on biofilm structure and behaviour." Thesis, University of Exeter, 1999. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.286538.

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Cui, Zhe. "Hydrodynamics in a bubble column at elevated pressures and turbulence energy distribution in bubbling gas-liquid and gas-liquid-solid flow systems." Connect to this title online, 2005. http://rave.ohiolink.edu/etdc/view?acc%5Fnum=osu1109956144.

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Thesis (Ph. D.)--Ohio State University, 2005.<br>Title from first page of PDF file. Document formatted into pages; contains xxiii, 187 p.; also includes graphics Includes bibliographical references (p. 179-187). Available online via OhioLINK's ETD Center
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Xie, Tao. "Hydrodynamic characteristics of gas/liquid/fiber three-phase flows based on objective and minimally-intrusive pressure fluctuation measurements." Diss., Available online, Georgia Institute of Technology, 2004:, 2004. http://etd.gatech.edu/theses/available/etd-09192004-033703/unrestricted/xie%5Ftao%5F200412%5Fphd.pdf.

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Thesis (Ph. D.)--Mechanical Engineering, Georgia Institute of Technology, 2005.<br>D. William Tedder, Committee Member ; Minami Yoda, Committee Member ; Tom McDonough, Committee Member ; Andrei G. Fedorov, Committee Member ; S. Mostafa Ghiaasiaan, Committee Chair ; Seppo Karrila, Committee Member. Includes bibliographical references.
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Van, Houwelingen ArJan. "Liquid-solid contacting in trickle-bed reactors." Thesis, University of Pretoria, 2009. http://hdl.handle.net/2263/30008.

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Several types of reactors are encountered in industry where reagents in a gas and a liquid phase need to be catalysed by a solid catalyst. Common reactors that are used to this end, are trickle-bed reactors, where gas and liquid flow cocurrently down a packed bed of catalyst. Apart from the catalytic process itself, several mass transfer steps can influence the rate and/or selectivity of a solid catalysed gas-liquid reaction. In trickle-bed reactors, flow morphology can have a major effect on these mass transfer steps. This study investigates the interaction between liquid flow morphology and
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Yang, Li. "CFD MODELING OF MULTIPHASE COUNTER-CURRENT FLOW IN PACKED BED REACTOR FOR CARBON CAPTURE." UKnowledge, 2015. http://uknowledge.uky.edu/me_etds/59.

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Packed bed reactors with counter-current, gas-liquid flows have been considered to be applicable in CO2 capture systems for post-combustion processing from fossil-fueled power production units. However, the hydrodynamics within the packing used in these reactors under counter-current flow has not been assessed to provide insight into design and operational parameters that may impact reactor and reaction efficiencies. Hence, experimental testing of a laboratory-scale spherical ball, packed bed with two-phase flow was accomplished and then a meso-scale 3D CFD model was developed to numerically s
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Serres, Marion. "Étude hydrodynamique d'un écoulement gaz-liquide dans un milieu poreux confiné." Thesis, Lyon, 2017. http://www.theses.fr/2017LYSEN018/document.

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Cette thèse se focalise sur les écoulements gaz-liquide dans un milieu poreux, problématique rencontrée dans des domaines variés allant de la physique fondamentale à la chimie appliquée. Nous avons caractérisé expérimentalement les régimes hydrodynamiques dans deux géométries différentes : un canal millifluidique (écoulement quasi-1D) et une cellule de Hele-Shaw (écoulement quasi-2D). L’originalité de ce travail est d’analyser l’effet du milieu poreux (lits de billes polydisperses ou mousses solides à cellules ouvertes), du confinement (1D/2D) et de la gravité en couplant des approches locales
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Barrios, Evelyn. "Hydrodynamique des reacteurs a lit fixe avec ecoulement en co-courant ascendant de gaz et de liquide." Paris 6, 1987. http://www.theses.fr/1987PA066066.

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L'etude experimentale porte sur plusieurs systemes : 4 types de solides (3 supports de catalyseur et des billes de verres, 2 liquides (eau ou cyclohexane) et 2 gaz (air ou azote) ainsi que 2 tailles de colonne (5 ou 15 cm). On suit l'influence de ces parametres sur le regime d'ecoulement, la retenue liquide et gazeuse et sur les pertes de charges
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Książki na temat "Hydrodynamics- Liquid flow"

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Yarin, Alexander L. Free liquid jets and films: Hydrodynamics and rheology. Longman Scientific & Technical, 1993.

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

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akov, V. E. Nakor i. Wave propagation in gas-liquid media. 2nd ed. CRC Press, 1993.

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Nakori͡akov, V. E. Wave propagation in gas-liquid media. 2nd ed. Edited by Pokusaev B. G, Shreĭber I. R, and Bergles A. E. 1935-. CRC Press, 1993.

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Franz-S, Rys, and Gyr Albert, eds. Physical processes and chemical reactions in liquid flows. A.A. Balkema, 1998.

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Computational hydrodynamics of capsules and biological cells. Chapman & Hall/CRC, 2010.

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Pozrikidis, C. Computational Hydrodynamics of Capsules and Biological Cells. Taylor & Francis Group, 2019.

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Części książek na temat "Hydrodynamics- Liquid flow"

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Nordsveen, Magnus, and Arnold F. Bertelsen. "Waves and Secondary Flows in Stratified Gas/Liquid Duct Flow." In Waves and Nonlinear Processes in Hydrodynamics. Springer Netherlands, 1996. http://dx.doi.org/10.1007/978-94-009-0253-4_22.

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Spielman, Lloyd A. "Flow Through Porous Media and Fluid-Particle Hydrodynamics." In Mathematical Models and Design Methods in Solid-Liquid Separation. Springer Netherlands, 1985. http://dx.doi.org/10.1007/978-94-009-5091-7_3.

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Simakov, Nikolay N. "Mathematical Modeling of Hydrodynamics of an Axisymmetric Two-Phase Flow Produced by a Nozzle." In Liquid Spray from Nozzles. Springer International Publishing, 2019. http://dx.doi.org/10.1007/978-3-030-12446-5_4.

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Li, Xiao-long, Ting-an Zhang, Yan Liu, Gui-li Liu, and Fang Dong. "Hydrodynamics of Gas–Liquid Two-Phase Flow in the Reverse Spray Washing Process." In Energy Technology 2021. Springer International Publishing, 2021. http://dx.doi.org/10.1007/978-3-030-65257-9_7.

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Kumitskiy, Boris, Svetlana Tul’skaya, Viktor Morozov, Egor Aralov, and Victor Budnikov. "Hydrodynamics of the Flow of an Ideal Liquid When It Flows Out of the Bottom Hole of a Parabolic Tank." In Lecture Notes in Civil Engineering. Springer International Publishing, 2022. http://dx.doi.org/10.1007/978-3-031-12703-8_22.

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Xu, Jinchao, Xiaodong Wang, Long Zhu, Donghui Zhou, and Jun Zhao. "Study on Air Bubble Plume in Open Channel with CFD-PBM Coupling Model." In Lecture Notes in Civil Engineering. Springer Nature Singapore, 2023. http://dx.doi.org/10.1007/978-981-19-6138-0_110.

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AbstractAir bubble plume flow has been applied widely in the dredging, ice breaking, and pollution control at navigation projects. But the interaction regimes among bubbles or between bubbles and water are not quite clear. Especially in open channels, the bubble plume flow are significantly affected by the separation phenomenon which is caused by the cross flow velocity. According to the existing research, the interaction force of gas-liquid and the distribution of bubble size are the key parameters to simulate the hydrodynamic characteristics of bubble plume flow. In order to explore the mechanism of air bubbles entrained plumes in open channels, an Eulerian-Eulerian approach for air-water flows numerical model was introduced, and the population balance model (PBM) was included to describe the distribution of bubble size. The cross flow velocity of open channels has been discussed in the proposed numerical model. It shows that the separation of bubble plume is strongly influenced by the cross flow velocity. The influence of these parameters on the movement characteristics of air bubbles is studied. The results indicate that the cross flow velocity has great impact on bubble plume as well as the lifting effectiveness of pneumatic sluicing. This research provides references for bubble plume in engineering applications.
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Akhatov, I. Sh, and R. G. Chembarisova. "The Thermoconvective Instability in Hydrodynamics of Relaxational Liquids." In Instabilities in Multiphase Flows. Springer US, 1993. http://dx.doi.org/10.1007/978-1-4899-1594-8_23.

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Tsaoulidis, Dimitrios A. "Liquid-Liquid Flows in Micro and Small Channels: Hydrodynamics and Pressure Drop." In Studies of Intensified Small-scale Processes for Liquid-Liquid Separations in Spent Nuclear Fuel Reprocessing. Springer International Publishing, 2015. http://dx.doi.org/10.1007/978-3-319-22587-6_4.

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Kalmbach, Thomas, Simon Gramlich, and Manfred Piesche. "Movement and Hydrodynamic Instabilities of Particle-Laden Liquid Jets in the Centrifugal Field Influenced by a Gas Flow." In Process-Spray. Springer International Publishing, 2016. http://dx.doi.org/10.1007/978-3-319-32370-1_5.

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Abiev, Rufat. "Analysis of Hydrodynamics and Mass Transfer of Gas-Liquid and Liquid-Liquid Taylor Flows in Microchannels." In Process Analysis, Design, and Intensification in Microfluidics and Chemical Engineering. IGI Global, 2019. http://dx.doi.org/10.4018/978-1-5225-7138-4.ch001.

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Analysis of hydrodynamics and mass transfer Taylor flows in micro channels of both gas-liquid and liquid-liquid systems on the basis of classical theoretical approach with some simplifying assumptions was performed. Results of theoretical analysis for description of hydrodynamic parameters and mass transfer characteristics were confirmed by comparison with the author's own and available in literature experimental data. It was shown that the main parameters of two-phase Taylor flows could be quite precisely described theoretically: mean bubble/droplet velocity, liquid film thickness, real gas holdup (which is always smaller than so-called dynamic holdup), pressure drop. Peculiarities of liquid-liquid flows compared to gas-liquid Taylor flows in capillaries are discussed. Wettability effect on hydrodynamics was examined. Tools of mass transfer intensification of gas-liquid and liquid-liquid Taylor flow in micro channels are analyzed. Three-layer model for heat and mass transfer has been proposed and implemented for the case of solid-liquid mass transfer for gas-liquid Taylor flows; optimal process conditions for this process are found theoretically and discussed from physical point of view.
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Streszczenia konferencji na temat "Hydrodynamics- Liquid flow"

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Borisov, I., A. Khalatov, and T. Wang. "Hydrodynamics of Rotating Bubble Flow." In ASME 2002 International Mechanical Engineering Congress and Exposition. ASMEDC, 2002. http://dx.doi.org/10.1115/imece2002-33832.

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This paper presents a new set of experimental data on the hydrodynamics of rotating bubble flow and is a continuation of previous gas-liquid rotating flow studies. The new data include the surface friction on both end walls of the vortex chamber, and static pressure distributions at the exit of swirl generator slots and on the inner surface of vortex chamber. The corotating disk technique was used to determine the friction momentum measured by the dynamometer. The air-liquid velocity was registered by the blade-anemometer with a light modulator fixed on its axis. The friction coefficient was f
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Khan, Wasim, Abhishek K. Chandra, Kaushal Kishor, Sadhana Sachan, and M. Siraj Alam. "Hydrodynamics and simulation studies of liquid-liquid slug flow in micro-capillaries." In 2017 International Conference on Advances in Mechanical, Industrial, Automation and Management Systems (AMIAMS). IEEE, 2017. http://dx.doi.org/10.1109/amiams.2017.8069225.

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Тутанина, Екатерина Михайловна, Антон Викторович Степыкин, and Елена Александровна Тарлаковская. "HYDRODYNAMICS OF LIQUID LAMINAR FILM FLOW ALONG MESH PACKING." In Поколение будущего: сборник избранных статей Международной студенческой научной конференции (Санкт-Петербург, Май 2022). Crossref, 2022. http://dx.doi.org/10.37539/pb197.2022.48.34.008.

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В статье приводятся уравнения распределения скорости по поверхности сетчатого элемента, при стекании жидкости в ламинарном режиме. Преобразование формул происходит на основе принятых допущений. Произведён анализ полученных уравнений и даны рекомендации к дальнейшему использованию. The article presents the equations of the velocity distribution over the surface of the mesh element, when the liquid flows in the laminar mode. The transformation of formulas takes place on the basis of accepted assumptions. The obtained equations are analyzed and recommendations for further use are given.
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Dittmar, Ina, and Peter Ehrhard. "On the Liquid/Liquid Slug Flow in a Micro-Capillary Reactor." In ASME 2014 12th International Conference on Nanochannels, Microchannels, and Minichannels collocated with the ASME 2014 4th Joint US-European Fluids Engineering Division Summer Meeting. American Society of Mechanical Engineers, 2014. http://dx.doi.org/10.1115/icnmm2014-21800.

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The hydrodynamics within a liquid/liquid slug flow in a micro-capillary reactor is characterized by complex vortex structures, both within the disperse and within the continuous phase. Usually, one of the phases exhibits good wetting of the wall, while the second phase exhibits poor wetting. This is why we expect a (continuous) thin film of the wetting phase along the wall. We compute this complex two-phase flow by means of a finite-volume method (FVM), whereas the interface is captured by a modified level-set method. Hence, from our numerical simulations we obtain the detailed topology of thi
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Gambaryan-Roisman, T., and P. Stephan. "Evaporation of Gravity- and Gas Flow-Driven Thin Liquid Films in Micro- and Minigrooves." In ASME 2004 2nd International Conference on Microchannels and Minichannels. ASMEDC, 2004. http://dx.doi.org/10.1115/icmm2004-2380.

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Using microstructured wall surfaces may improve the heat transfer performance of falling film or shear-driven film cooling devices enormously. The advantages of the structured surface include the prevention of the formation of dry patches on hot surfaces, the promotion of ultra-thin film evaporation, and a wavy motion of the film that enhances mixing of the liquid. We develop a model describing the hydrodynamics and heat transfer by evaporation of gravity- and gas flow-driven liquid films on grooved surfaces. For low Reynolds numbers or low liquid mass fluxes the heat transfer is governed by t
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Oladyshkin, S., and M. Panfilov. "Splitting the Thermodynamlics and Hydrodynamics in Compositional Gas-Liquid Flow through Porous Reservoirs." In ECMOR X - 10th European Conference on the Mathematics of Oil Recovery. European Association of Geoscientists & Engineers, 2006. http://dx.doi.org/10.3997/2214-4609.201402528.

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Tan, M., P. Temarel, S. H. Miao, and Y. B. Lee. "Coupling Between Flexible Ship and Liquid Sloshing Using Potential Flow Analysis and its Effect on Wave-Induced Loads." In William Froude Conference: Advances in Theoretical and Applied Hydrodynamics - Past And Future. RINA, 2010. http://dx.doi.org/10.3940/rina.wfa.2010.08.

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Etminan, Amin, Yuri S. Muzychka, and Kevin Pope. "CFD Modelling for Gas-Liquid and Liquid-Liquid Taylor Flows in the Entrance Region of Microchannels." In ASME 2021 Fluids Engineering Division Summer Meeting. American Society of Mechanical Engineers, 2021. http://dx.doi.org/10.1115/fedsm2021-64172.

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Abstract This paper presents a CFD-based simulation method for air/water and water/dodecane Taylor flows through an axisymmetric microchannel with a circular cross-sectional area. A systematic analysis is conducted by exploring the effects of different superficial velocities and apparent viscosities on the hydrodynamics of a slug flow regime. A concentric junction is employed to make bubbles of air in a continuous flow of water and slugs of water in a continuous flow of dodecane oil. A time-history study is conducted to predict the air-bubble and water-slug evolution processes, in particular a
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Kurnia, Jundika Candra, Imen ben Salem, Humair Nadeem, Tariq Shamim, and Mohamed Sassi. "Numerical Investigation of Multiphase Flow Hydrodynamics in Trickle Bed Reactors." In ASME 2014 4th Joint US-European Fluids Engineering Division Summer Meeting collocated with the ASME 2014 12th International Conference on Nanochannels, Microchannels, and Minichannels. American Society of Mechanical Engineers, 2014. http://dx.doi.org/10.1115/fedsm2014-22152.

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For decades, trickle bed reactors (TBRs) have been widely used in chemical process industries due to their cost effectiveness and simplicity in operation. Despite their wide use, designing efficient TBRs is challenging, considering the complexity of various transport processes and interactions that occur simultaneously in TBRs. Hence, it is of prime importance to have a comprehensive understanding on the multiphase flow inside TBRs. The objective of this study is to investigate hydrodynamic of multiphase flow and to identify the flow regime developed inside TBRs. Multiphase flow inside TBRs is
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Gera, Dinesh, Madhava Syamlal, and Thomas J. O’Brien. "Hydrodynamics of Multiple Size Particles in a Liquid Fluidized Bed Classifier." In ASME/JSME 2003 4th Joint Fluids Summer Engineering Conference. ASMEDC, 2003. http://dx.doi.org/10.1115/fedsm2003-45494.

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A two fluid model is extended to an N-phase, multi-fluid model, in which each particulate phase represents a collection of particles with identical diameter and density. The current N-phase model is applied to a fluidized bed classifier with six different particle sizes to investigate the effects of different operating conditions—fluidizing liquid flow rate, feed voidage, and particle size distribution in the feed stream—on the particle size distribution inside the classifier and the discharge streams. The predicted volume fraction of different particle sizes is compared with the experimental
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Raporty organizacyjne na temat "Hydrodynamics- Liquid flow"

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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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