Добірка наукової літератури з теми "Gas-liquid-solid flows"
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Статті в журналах з теми "Gas-liquid-solid flows"
KAWASAKI, Koji, and Keji NAKATSUJI. "NUMERICAL EXPERIMENT OF GAS-LIQUID PHASE AND SOLID-GAS-LIQUID PHASE FLOWS." PROCEEDINGS OF HYDRAULIC ENGINEERING 46 (2002): 1049–54. http://dx.doi.org/10.2208/prohe.46.1049.
Повний текст джерелаDouek, R. S., G. F. Hewitt, and A. G. Livingston. "Hydrodynamics of vertical co-current gas-liquid-solid flows." Chemical Engineering Science 52, no. 23 (December 1997): 4357–72. http://dx.doi.org/10.1016/s0009-2509(97)00182-6.
Повний текст джерелаKITAHARA, Hiroyuki, and Kunio YOSHIDA. "Flow Patterns for Gas-Liquid and Gas-Liquid-Solid Flows in a Vertical Pipe." JAPANESE JOURNAL OF MULTIPHASE FLOW 3, no. 2 (1989): 145–54. http://dx.doi.org/10.3811/jjmf.3.145.
Повний текст джерелаLee, Y. J., and J. H. Kim. "A Review of Holography Applications in Multiphase Flow Visualization Study." Journal of Fluids Engineering 108, no. 3 (September 1, 1986): 279–88. http://dx.doi.org/10.1115/1.3242575.
Повний текст джерелаSassi, Paolo, Youssef Stiriba, Julia Lobera, Virginia Palero, and Jordi Pallarès. "Experimental Analysis of Gas–Liquid–Solid Three-Phase Flows in Horizontal Pipelines." Flow, Turbulence and Combustion 105, no. 4 (May 9, 2020): 1035–54. http://dx.doi.org/10.1007/s10494-020-00141-1.
Повний текст джерелаSilapov, Begench, and Iulian Nistor. "MOVEMENT OF TWO-PHASE GAS-LIQUID FLOW IN HORIZONTAL AND INCLINED PIPES." Romanian Journal of Petroleum & Gas Technology 4 (75), no. 1 (2023): 61–72. http://dx.doi.org/10.51865/jpgt.2023.01.06.
Повний текст джерелаRampure, Mohan R., Vivek V. Buwa, and Vivek V. Ranade. "Modelling of Gas-Liquid/Gas-Liquid-Solid Flows in Bubble Columns: Experiments and CFD Simulations." Canadian Journal of Chemical Engineering 81, no. 3-4 (May 19, 2008): 692–706. http://dx.doi.org/10.1002/cjce.5450810348.
Повний текст джерелаBaltussen, M. W., L. J. H. Seelen, J. A. M. Kuipers, and N. G. Deen. "Direct Numerical Simulations of gas–liquid–solid three phase flows." Chemical Engineering Science 100 (August 2013): 293–99. http://dx.doi.org/10.1016/j.ces.2013.02.052.
Повний текст джерелаHosokawa, Shigeo, and Akio Tomiyama. "Turbulence modification in gas–liquid and solid–liquid dispersed two-phase pipe flows." International Journal of Heat and Fluid Flow 25, no. 3 (June 2004): 489–98. http://dx.doi.org/10.1016/j.ijheatfluidflow.2004.02.001.
Повний текст джерелаHegab, A. M., S. A. Gutub, and A. Balabel. "A Developed Numerical Method for Turbulent Unsteady Fluid Flow in Two-Phase Systems with Moving Interface." International Journal of Computational Methods 14, no. 06 (August 2017): 1750063. http://dx.doi.org/10.1142/s0219876217500633.
Повний текст джерелаДисертації з теми "Gas-liquid-solid flows"
Cai, Xuan [Verfasser], and B. [Akademischer Betreuer] Frohnapfel. "Interface-Resolving Simulations of Gas-Liquid Two-Phase Flows in Solid Structures of Different Wettability / Xuan Cai ; Betreuer: B. Frohnapfel." Karlsruhe : KIT-Bibliothek, 2016. http://d-nb.info/1126036811/34.
Повний текст джерелаLiu, Yefei [Verfasser], Kai-Olaf [Akademischer Betreuer] Hinrichsen, and Ville R. I. [Akademischer Betreuer] Kaila. "Two-fluid modeling of gas-solid and gas-liquid flows: Solver development and application / Yefei Liu. Gutachter: Kai-Olaf Hinrichsen ; Ville R. I. Kaila. Betreuer: Kai-Olaf Hinrichsen." München : Universitätsbibliothek der TU München, 2014. http://d-nb.info/1059477254/34.
Повний текст джерелаBogner, Simon [Verfasser], Ulrich [Gutachter] Rüde, Manfred [Gutachter] Krafczyk, and Jens [Gutachter] Harting. "Direct Numerical Simulation of Liquid-Gas-Solid Flows Based on the Lattice Boltzmann Method / Simon Bogner ; Gutachter: Ulrich Rüde, Manfred Krafczyk, Jens Harting." Erlangen : Friedrich-Alexander-Universität Erlangen-Nürnberg (FAU), 2017. http://d-nb.info/1139171534/34.
Повний текст джерелаSassi, Arobba Paolo Juan. "Experimental analysis of multiphase flows. Design and setup of an experimental facility." Doctoral thesis, Universitat Rovira i Virgili, 2021. http://hdl.handle.net/10803/671990.
Повний текст джерелаLa dinámica de los flujos trifásicos se rige por fenómenos de alta complejidad, tanto conceptual como matemática. Una mejor comprensión así como un incremento en la capacidad de predicción de su dinámica, son cruciales para el diseño y construcción de instalaciones de interés para una amplia gama de industrias. Este trabajo de investigación presenta el diseño y montaje de LESLIE, un circuito cerrado de baja presión destinado a la investigación experimental de la dinámica de flujos bifásicos y trifásicos a través de tuberías y sus accesorios. LESLIE está pensado para obtener medidas de parámetros clave y caracterizar flujos multifásicos con fases gaseosas, líquidas y sólidas, tanto en tuberías horizontales como verticales.Presentamos aquí nuevos datos experimentales para regímenes intermitentes en flujos bifásicos y trifásicos en configuración horizontal usando aire, agua y partículas de polipropileno con tamaños de entre 1 y 2 milímetros. Visualizaciones del flujo, medidas de presión y fracción de vacío se han obtenido para diferentes condiciones de operación de flujos intermitentes. En este trabajo investigamos el impacto de la presencia de partículas sólidas sobre la caída de presión, el régimen de flujo y la frecuencia del "slug". Además, el análisis del comportamiento de flujos bifásicos anulares mediante técnicas de procesado de imágenes ha permitido obtener resultados sobre la distribución de tamaño de partícula, las cuales también se presentan en este trabajo.
The dynamics of three-phase flows involve phenomena of high complexity, whose understanding and an enhanced prediction capacity of fluid dynamics in multiphase flow systems is crucial for the design and construction of facilities meant for a wide range of industries. This research work presents the design and set up of LESLIE, a low pressure multiphase flow loop for the experimental analysis of two and three-phase flows through pipelines and their accessories. It is designed to measure key parameters, so as to characterise the behaviour of multiphase flows involving gas, liquid and solid phases both in horizontal and vertical pipelines. New experimental data is presented in this study for intermittent two and three-phase flows in horizontal pipelines involving air, water and polypropylene pellets of sizes ranging between 1 and 2 millimetres. Flow visualization, pressure and void fraction measurements were performed and are explored in this work for the case of intermittent flows for a variety of settings. The influence of solid particles over the frictional pressure drop, flow regime and slug frequency is reported in this work. Furthermore, the analysis of the dynamics of annular two-phase flows by means of image processing techniques has allowed obtaining droplet size distributions, which are also presented in this study.
Dong, Xuefeng Materials Science & Engineering Faculty of Science UNSW. "Modelling of gas-powder-liquid-solid multiphase flow in a blast furnace." Awarded by:University of New South Wales. School of Materials Science and Engineering, 2004. http://handle.unsw.edu.au/1959.4/20808.
Повний текст джерелаCui, 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.
Повний текст джерелаTitle 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
Rapisarda, Andrea. "Hydrodynamic characterization of two/three phase flow regimes in stirred tank." Master's thesis, Alma Mater Studiorum - Università di Bologna, 2019.
Знайти повний текст джерелаLiedtke, Anne-Kathrin. "Study of a new gas-liquid-solid three phase contact mode at millimetric scale : catalytic reactors using “slurry Taylor” flow." Thesis, Lyon 1, 2014. http://www.theses.fr/2014LYO10137/document.
Повний текст джерелаSlurry reactors, widely encountered in chemical industry (laboratory scale up to manufactaring), offer good mass and heat transfer capacities and their high flexibility ensures the simple changeover of solid phases enables a continuous online fresh catalyst feed for fast deactivating catalysts. However slurry reactors promote a high degree of backmixing which can be a drawback for reactions with selectivity issues or when very high conversions are required. In microreaction technology, Taylor flow is often employed providing excellent heat and mass transfer and almost ideal plug flow behavior. Solid handing in these small structures is often resolved by immobilizing the solid catalyst which impinges on the flexibility. One possible solution to combine beneficial properties of Taylor flow with the operational flexibility of conventional slurry reactors is a “slurry Taylor” flow (STF) where catalyst particles are suspended and kept in motion by the internal circulations present in the liquid slugs. The focus of this work is the design and characterization of this innovative gas-liquid-solid contactor. Particles were transported in millimetric horizontal and vertical tubing without the risk of clogging. Hydrodynamic studies revealed different flow patterns depending mainly on velocity and flow orientation. Ion exchange resin particles were used to study the liquid-solid mass transfer and first correlation for the Sherwood number in STF is proposed
Serres, Marion. "Étude hydrodynamique d'un écoulement gaz-liquide dans un milieu poreux confiné." Thesis, Lyon, 2017. http://www.theses.fr/2017LYSEN018/document.
Повний текст джерелаThis thesis focuses on gas-liquid flow in porous media, a common problem encountered in various domains from fundamental physics to applied chemical engineering. We have characterized the hydrodynamic regimes based on two different experimental devices geometry: a millichannel (1D flow) and a Hele-Shaw cell (2D flow). The originality of this work is to analyze the influence of the porous medium (monodisperse micro-packed beds or open cell solid foams), confinement (1D/2D) and gravity by coupling global and local analysis from either chemical engineering or fundamental physics community. On the one hand, a global analysis made it possible to quantify pressure drops, residence time distributions (RTD) based on fluorescent dye transport and gas-liquid mass transfer on the 1D device. On the other hand, a local analysis of the liquid fraction and the spatio-temporal evolution of its frequency pointed out the existence of two hydrodynamic regimes: a Taylor-like regime in which the characteristics of the periodic flow upstream are conserved in the porous medium and a modulated regime characterized by the flow disorganization at the porous medium entrance. A phenomenological model is developed based on bubbles propagation inside the medium and reproduces well both regimes. These two analyses are finally coupled to study multiphase flows inside the Hele-Shaw cell. The effects of gravity and confinement are discussed
Braga, Maria. "Étude des phénomènes de transfert et de l'hydrodynamique dans des réacteurs agités à panier catalytique." Thesis, Lyon 1, 2014. http://www.theses.fr/2014LYO10011/document.
Повний текст джерелаStationary catalytic basket stirred reactors are often used among the various three-phase laboratory reactors for primary screening of commercial shaped catalysts. Until today, hydrodynamics and mass transfer studies concerning the impact of the presence of the basket in the flow are scarce which can be an obstacle to catalyst screening mainly in the case of fast reactions. The aim of this study is to know the range of applicability of these devices and optimize them if necessary. A characterization methodology that couples hydrodynamics and mass transfer was developed. The hydrodynamic studies allowed establishing a flow regime map of the gas/liquid flow for different reactor designs and operational conditions. This study has allowed as well understanding the influence of the basket and gas bubbles on gas/liquid and solid/liquid mass transfer. For the studied reactor, the liquid/solid mass transfer is the limiting phenomena. This system can however be used for catalyst screening for reaction rate constants smaller than 0.02 s-1. For faster reactions, these devices must be improved by changing the design of basket and impeller and the tank diameter. The optimized configuration should improve de radial flow through the porous medium and avoid the flow bypassing around the basket
Частини книг з теми "Gas-liquid-solid flows"
Bourloutski, E., and M. Sommerfeld. "Euler/Lagrange Calculations of Gas-Liquid-Solid-Flows in Bubble Columns with Phase Interaction." In Bubbly Flows, 243–59. Berlin, Heidelberg: Springer Berlin Heidelberg, 2004. http://dx.doi.org/10.1007/978-3-642-18540-3_19.
Повний текст джерелаValentine, Brian G. "Multiphase Flow Phenomena (Gas/Solid and Gas/Liquid Systems)." In Mechanical Engineering Series, 77–95. Cham: Springer International Publishing, 2021. http://dx.doi.org/10.1007/978-3-030-68578-2_3.
Повний текст джерелаPandit, Aniruddha. "Multiphase Phenomena and Design of Gas-Solid-Liquid Stirred Tanks." In Handbook of Multiphase Flow Science and Technology, 1–41. Singapore: Springer Nature Singapore, 2023. http://dx.doi.org/10.1007/978-981-4585-86-6_50-1.
Повний текст джерелаCavalli, Stella, Rafael F. Alves, Carlos L. Bassani, Eduardo Nunes dos Santos, Marco da Silva, Moises A. Marcelino Neto, Amadeu K. Sum, and Rigoberto E. M. Morales. "Experimental Analysis of Three-Phase Solid-Liquid-Gas Slug Flow with Hydrate-Like Particles." In Lecture Notes in Mechanical Engineering, 267–73. Cham: Springer International Publishing, 2022. http://dx.doi.org/10.1007/978-3-030-93456-9_24.
Повний текст джерелаYonemoto, Yukihiro, and Tomoaki Kunugi. "Multi-scale Multiphase Flow Gas–Liquid–Solid Interfacial Equation Based on Thermodynamic and Mathematical Approach." In The Surface Wettability Effect on Phase Change, 317–41. Cham: Springer International Publishing, 2022. http://dx.doi.org/10.1007/978-3-030-82992-6_11.
Повний текст джерелаHou, Rong Guo, Chuan Zhen Huang, Jun Wang, Hong Tao Zhu, and Yan Xia Feng. "Simulation of Gas-Solid-Liquid Three-Phase Flow Inside and Outside the Abrasive Water Jet Nozzle." In Materials Science Forum, 833–36. Stafa: Trans Tech Publications Ltd., 2006. http://dx.doi.org/10.4028/0-87849-421-9.833.
Повний текст джерелаHou, Rong Guo, Chuan Zhen Huang, Li Li, Zong Wei Niu, and Zhi Yong Li. "Simulation of the Gas-Liquid-Solid Three-Phase Flow Velocity Field Outside the Abrasive Water Jet(AWJ) Rectangle Nozzle and Ellipse Nozzle." In Advances in Grinding and Abrasive Technology XIV, 470–73. Stafa: Trans Tech Publications Ltd., 2007. http://dx.doi.org/10.4028/0-87849-459-6.470.
Повний текст джерелаAbiev, 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, 1–49. IGI Global, 2019. http://dx.doi.org/10.4018/978-1-5225-7138-4.ch001.
Повний текст джерелаYabe, Takashi, Youichi Ogata, and Takao Kawai. "Simulation of Structure-Fluid Interaction by Universal Solver CIP for Solid, Liquid and Gas in Cartesian Grid." In Numerical Simulations of Incompressible Flows, 340–49. WORLD SCIENTIFIC, 2003. http://dx.doi.org/10.1142/9789812796837_0020.
Повний текст джерела"Flow of Gas, Liquid and Solid." In Blast Furnace Phenomena and Modelling, 297–413. Dordrecht: Springer Netherlands, 1987. http://dx.doi.org/10.1007/978-94-009-3431-3_4.
Повний текст джерелаТези доповідей конференцій з теми "Gas-liquid-solid flows"
Zhang, Xinyu, and Goodarz Ahmadi. "Particle Effects on Gas-Liquid-Solid Flows." In ASME 2011 International Mechanical Engineering Congress and Exposition. ASMEDC, 2011. http://dx.doi.org/10.1115/imece2011-65695.
Повний текст джерелаLiu, Xijie, Yap Yit Fatt, and Sami Ainane. "CFD Modeling of Erosion in Gas-Solid and Liquid-Solid Flows." In RDPETRO 2018: Research and Development Petroleum Conference and Exhibition, Abu Dhabi, UAE, 9-10 May 2018. American Association of Petroleum Geologists, Society of Exploration Geophysicists, European Association of Geoscientists and Engineers, and Society of Petroleum Engineers, 2018. http://dx.doi.org/10.1190/rdp2018-41921364.1.
Повний текст джерелаHosokawa, Shigeo, and Akio Tomiyama. "TURBULENCE MODIFICATION IN GAS-LIQUID AND SOLID-LIQUID DISPERSED TWO-PHASE PIPE FLOWS." In Third Symposium on Turbulence and Shear Flow Phenomena. Connecticut: Begellhouse, 2003. http://dx.doi.org/10.1615/tsfp3.330.
Повний текст джерелаZhang, Xinyu, and Goodarz Ahmadi. "Roles of Neutrally Buoyant Particles in Gas-Liquid-Solid 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/fedsm2012-72038.
Повний текст джерелаAhmadi, Goodarz, and Xinyu Zhang. "Three-Phase Liquid-Gas-Solid Flows in a Bubble Column." In ASME 2005 Fluids Engineering Division Summer Meeting. ASMEDC, 2005. http://dx.doi.org/10.1115/fedsm2005-77071.
Повний текст джерелаZhang, Xinyu, and Goodarz Ahmadi. "Effects of Neutrally Buoyant Particles on Gas-Liquid-Solid Flows." In ASME 2013 Fluids Engineering Division Summer Meeting. ASME, 2013. http://dx.doi.org/10.1115/fedsm2013-16299.
Повний текст джерелаSedrez, Thiana A., and Siamack A. Shirazi. "The Effect of Phase Interaction Forces and Particle Rotation on Solid Particle Erosion in Liquid-Solid and Liquid-Gas-Solid Flows." In ASME 2022 Fluids Engineering Division Summer Meeting. American Society of Mechanical Engineers, 2022. http://dx.doi.org/10.1115/fedsm2022-86755.
Повний текст джерелаMusavian, S. M., and A. F. Najafi. "Numerical Simulations of Gas-Liquid-Solid Flows in a Hydrocyclone Separator." In ASME/JSME 2007 5th Joint Fluids Engineering Conference. ASMEDC, 2007. http://dx.doi.org/10.1115/fedsm2007-37374.
Повний текст джерелаSakaguchi, Tadashi, H. Minagawa, K. Sahara, and T. Saibe. "ESTIMATION OF VOLUMETRIC FRACTIONS OF EACH PHASE IN GAS-LIQUID-SOLID THREE-PHASE SLUG FLOW IN VERTICAL PIPES." In Dynamics of Two-Phase Flows. Connecticut: Begellhouse, 2023. http://dx.doi.org/10.1615/0-8493-9925-4.40.
Повний текст джерелаZhang, Xinyu, and Goodarz Ahmadi. "Effects of Particle Density on Gas-Liquid-Solid Flows in Bubble Columns." 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/fedsm2014-21082.
Повний текст джерелаЗвіти організацій з теми "Gas-liquid-solid flows"
Liu, D., and T. de Bruin. New technology for fluid dynamic measurements in gas-liquid-solid three-phase flow reactors. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1991. http://dx.doi.org/10.4095/304508.
Повний текст джерелаSvedeman. L51729 Gas Scrubber Performance Evaluation - Measurement Methods. Chantilly, Virginia: Pipeline Research Council International, Inc. (PRCI), April 1995. http://dx.doi.org/10.55274/r0010420.
Повний текст джерелаSnyder, Victor A., Dani Or, Amos Hadas, and S. Assouline. Characterization of Post-Tillage Soil Fragmentation and Rejoining Affecting Soil Pore Space Evolution and Transport Properties. United States Department of Agriculture, April 2002. http://dx.doi.org/10.32747/2002.7580670.bard.
Повний текст джерелаLahav, Ori, Albert Heber, and David Broday. Elimination of emissions of ammonia and hydrogen sulfide from confined animal and feeding operations (CAFO) using an adsorption/liquid-redox process with biological regeneration. United States Department of Agriculture, March 2008. http://dx.doi.org/10.32747/2008.7695589.bard.
Повний текст джерела