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Статті в журналах з теми "Fluid flow and heat transfer"

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Coulson, J. M., J. F. Richardson, J. R. Backhurst, and J. H. Harker. "Fluid flow, heat transfer and mass transfer." Filtration & Separation 33, no. 2 (February 1996): 102. http://dx.doi.org/10.1016/s0015-1882(96)90353-5.

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Makinde, O. D., R. J. Moitsheki, R. N. Jana, B. H. Bradshaw-Hajek, and W. A. Khan. "Nonlinear Fluid Flow and Heat Transfer." Advances in Mathematical Physics 2014 (2014): 1–2. http://dx.doi.org/10.1155/2014/719102.

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Muthusamy, P., and Palanisamy Senthil Kumar. "Waste Heat Recovery Using Matrix Heat Exchanger from the Exhaust of an Automobile Engine for Heating Car’s Passenger Cabin." Advanced Materials Research 984-985 (July 2014): 1132–37. http://dx.doi.org/10.4028/www.scientific.net/amr.984-985.1132.

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The main objective of our work is to analysis the heat transfer rate for various fluids with different matrix heat exchanger (MHE) models and flow characteristic in matrix heat exchanger by using computational fluid dynamics (CFD) package with small car. The amount of heat carried by the cold fluid from hot fluid is mainly depends upon the mass flow rate of the working fluid. The heat transfer area per unit volume of tube is more. So, it increases the temperature of the cold fluid. Here, the hot and cold fluids are moving in the alternate tubes of heat exchanger in the counter flow direction. The small amounts of pressure drop are occurred but which is less compared to existing model. Flow disturbances are rectified in the MHE through the modifications made. Since, silicon carbide material is used as a polishing material to avoid the deposit of carbon at the inner side of the flow passage and this waste heat energy is used for heating passenger cabin during winter season. The wood is used as an insulating material to avoid the heat flow from fluid to atmosphere. Keywords-Heat transfer rate, Matrix heat exchanger, Working fluid, Polishing material.
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Nallusamy, S. "Characterization of Al2O3/Water Nanofluid through Shell and Tube Heat Exchangers over Parallel and Counter Flow." Journal of Nano Research 45 (January 2017): 155–63. http://dx.doi.org/10.4028/www.scientific.net/jnanor.45.155.

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Nanotechnology has become one of the fastest growing scientific and engineering disciplines. Nano fluids have been established to possess enhanced thermal and physical properties such as thermal conductivity, thermal diffusivity, viscosity and convective heat transfer coefficients. The aim of this research article is to analyze the overall heat transfer coefficient by doing an experimental investigation on the convective heat transfer and flow characteristics of a nano fluid. In this research, an attempt was made for the nano fluid consisting of water and 1% volume concentration of Al2O3/water Nano fluid flowing in a parallel flow, counter flow in shell and tube heat exchanger under laminar flow condition. The 50nm diameter Al2O3nanoparticles are used in this investigation and was found that the overall heat transfer coefficient and convective heat transfer coefficient of nano fluid to be slightly higher than that of the base liquid at same mass flow rate and inlet temperature. Three samples of dissimilar mass flow rates have been identified for conducting the experiments and their results are continuously monitored and reported. The experimental analysis results were concluded that the heat transfer and overall heat transfer coefficient enhancement is possible with increase in the mass flow rate of fluid and Al2O3/water nano fluid on a comparative basis.
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Rao, H. V. "Isentropic recuperative heat exchanger with regenerative work transfer." Proceedings of the Institution of Mechanical Engineers, Part C: Journal of Mechanical Engineering Science 214, no. 4 (April 1, 2000): 609–18. http://dx.doi.org/10.1243/0954406001523948.

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A counter-flow heat exchanger is considered to be the ideal method for recuperative heat transfer between hot and cold fluid streams. In this paper the concept of an isentropic heat exchanger with regenerative work transfer is developed. The overall effect is a mutual heat transfer between the two fluid streams without any net external heat or work transfers. The effectiveness for an isentropic heat exchanger with regenerative work transfer is derived for the case of fluid streams with constant specific heats and it is shown that it is greater than unity. The ‘isentropic effectiveness’ of a heat exchanger is defined. The relationship between the entropy generation and effectiveness for the traditional heat exchanger is also examined and compared with that of the isentropic heat exchanger. The practical realization of isentropic operation of a heat exchanger and its possible application are briefly considered.
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Rajavel, Rangasamy, and Kaliannagounder Saravanan. "Heat transfer studies on spiral plate heat exchanger." Thermal Science 12, no. 3 (2008): 85–90. http://dx.doi.org/10.2298/tsci0803085r.

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In this paper, the heat transfer coefficients in a spiral plate heat exchanger are investigated. The test section consists of a plate of width 0.3150 m, thickness 0.001 m and mean hydraulic diameter of 0.01 m. The mass flow rate of hot water (hot fluid) is varying from 0.5 to 0.8 kg/s and the mass flow rate of cold water (cold fluid) varies from 0.4 to 0.7 kg/s. Experiments have been conducted by varying the mass flow rate, temperature, and pressure of cold fluid, keeping the mass flow rate of hot fluid constant. The effects of relevant parameters on spiral plate heat exchanger are investigated. The data obtained from the experimental study are compared with the theoretical data. Besides, a new correlation for the Nusselt number which can be used for practical applications is proposed.
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KIMURA, Fumiyoshi, and Kenzo KITAMURA. "A304 FLUID FLOW AND HEAT TRANSFER OF NATURAL CONVECTION ADJACENT TO UPWARD-FACING, INCLINED, HEATED PLATE : AIR CASE(Heat Transfer-1)." Proceedings of the International Conference on Power Engineering (ICOPE) 2009.3 (2009): _3–19_—_3–24_. http://dx.doi.org/10.1299/jsmeicope.2009.3._3-19_.

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Zhou, Guo Fa, and Ting Peng. "Heat Transfer Enhancement of Viscoelastic Fluid in the Rectangle Microchannel with Constant Heat Fluxes." Applied Mechanics and Materials 117-119 (October 2011): 574–81. http://dx.doi.org/10.4028/www.scientific.net/amm.117-119.574.

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Анотація:
It has been found that viscoelastic fluid has evident heat transfer enhancement function in macro scale. But in micro scale, viscoelastic fluid’s flow and heat transfer characteristics are still unknown. In this paper, the heat transfer process of viscoelastic fluid in the microchannel is studied by numerical simulation method. The simulation results show that the maximum heat transfer enhancement of viscoelastic fluid is up to 800%, compared with pure viscous fluid. The viscoelastic fluid has such obvious heat transfer enhancement function because of its strong secondary flow. Laminar sub-layer can be damaged by the strong secondary flow, and thus radial flow generates in laminar sub-layer. The radial flow can increase the interference and mixing effect, and enhances fluid’s turbulence and convection which can enhance heat transfer as a result. So the heat transfer enhancement depends on the intensity of secondary flow which is caused by the second normal stress difference, and it will increase with the raise of the flow rate.
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Yue, Qingwen, Xide Lai, Xiaoming Chen, and Ping Hu. "Study on heat transfer characteristics of flow heat coupling of horizontal spiral tube heat exchanger." Thermal Science and Engineering 4, no. 2 (September 10, 2021): 23. http://dx.doi.org/10.24294/tse.v4i2.1516.

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In view of the complex structural characteristics and special operating environment of the horizontal spiral tube heat exchanger of the shaft sealed nuclear main pump, the numerical simulation method of flow heat coupling is used to analyze the influence of the flow and temperature changes of the fluid on the shell side on the flow field and temperature field of the heat exchanger, explore the influence rules of the inlet parameters on the flow and heat transfer characteristics of the fluid in the heat exchanger, and analyze the enhanced heat transfer performance of the heat exchanger by using the relevant heat transfer criteria. The results show that the horizontal spiral tube fluid generates centrifugal force under the influence of curvature, forming a secondary flow which is different from the straight tube flow heat transfer, and the velocity distribution is concave arc, which will enhance the heat transfer efficiency of the heat exchanger; with the increase of shell side velocity, the degree of fluid disturbance and turbulence increases, while the pressure loss does not change significantly, and the heat transfer performance of the heat exchanger increases; under the given structure and size, the heat transfer performance curve of the heat exchanger shows that the increase of shell side flow and Reynolds number has a significant impact on the enhanced heat transfer of the spiral tube. In practical engineering applications, the heat transfer can be strengthened by appropriately increasing the shell side flow of the heat exchanger.
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Corzo, Santiago Francisco, Damian Enrique Ramajo, and Norberto Marcelo Nigro. "High-Rayleigh heat transfer flow." International Journal of Numerical Methods for Heat & Fluid Flow 27, no. 9 (September 4, 2017): 1928–54. http://dx.doi.org/10.1108/hff-05-2016-0176.

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Purpose The purpose of this paper is to assess the Boussinesq approach for a wide range of Ra (10 × 6 to 10 × 11) in two-dimensional (square cavity) and three-dimensional (cubic cavity) problems for air- and liquid-filled domains. Design/methodology/approach The thermal behavior in “differentially heated cavities” filled with air (low and medium Rayleigh) and water (high Rayleigh) is solved using computational fluid dynamics (CFDs) (OpenFOAM) with a non-compressible (Boussinesq) and compressible approach (real water properties from the IAPWS database). Findings The results from the wide range of Rayleigh numbers allowed for the establishment of the limitation of the Boussinesq approach in problems where the fluid has significant density changes within the operation temperature range and especially when the dependence of density with temperature is not linear. For these cases, the symmetry behavior predicted by Boussinesq is far from the compressible results, thus inducing a transient heat imbalance and leading to a higher mean temperature. Research limitations/implications The main limitation of the present research can be found in the shortage of experimental data for very high Rayleigh problems. Practical implications Practical implications of the current research could be use of the Boussinesq approach by carefully observing its limitations, especially for sensible problems such as the study of pressure vessels, nuclear reactors, etc. Originality/value The originality of this paper lies in addressing the limitations of the Boussinesq approach for high Rayleigh water systems. This fluid is commonly used in numerous industrial equipment. This work presents valuable conclusions about the limitations of the currently used models to carry out industrial simulations.
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Дисертації з теми "Fluid flow and heat transfer"

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Mala, Gh Mohiuddin. "Heat transfer and fluid flow in microchannels." Thesis, National Library of Canada = Bibliothèque nationale du Canada, 1999. http://www.collectionscanada.ca/obj/s4/f2/dsk1/tape8/PQDD_0005/NQ39562.pdf.

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Beale, Steven Brydon. "Fluid flow and heat transfer in tube banks." Thesis, Imperial College London, 1992. http://hdl.handle.net/10044/1/8103.

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Tian, Jing. "Fluid flow and heat transfer in woven textiles." Thesis, University of Cambridge, 2005. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.615243.

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Matys, Paul. "Fluid flow and heat transfer in continuous casting processes." Thesis, University of British Columbia, 1988. http://hdl.handle.net/2429/28504.

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A three-dimensional finite difference code was developed to simulate fluid flow and heat transfer phenomena in continuous casting processes. The mathematical model describes steady state transport phenomena in a three dimensional solution domain that involves: turbulent fluid flow, natural and forced convection, conduction, release of latent heat at the solidus surface, and tracing of unknown location of liquid/solid interface. The governing differential equations are discretized using a finite volume method and a hybrid central, upwind differencing scheme. A fully three-dimensional ADI-like iterative procedure is used to solve the discretized algebraic equations for each dependent variable. The whole system of interlinked equations is solved by the SIMPLE algorithm. The developed computer code was used for parametric studies of continuous casting of aluminum. The results were compared against available experimental data. This numerical simulation enhances understanding of the fluid flow and heat transfer phenomena in continuous casting processes and can be used as a tool to optimize technologies for continuous casting of metals.
Applied Science, Faculty of
Mechanical Engineering, Department of
Graduate
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Janakiraman, S. V. "Fluid flow and heat transfer in transonic turbine cascades." Thesis, This resource online, 1993. http://scholar.lib.vt.edu/theses/available/etd-06112009-063614/.

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McPhail, Stephen John. "Single-phase fluid flow and heat transfer in microtubes." [S.l. : s.n.], 2008. http://nbn-resolving.de/urn:nbn:de:bsz:93-opus-36182.

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Jagannatha, Deepak. "Heat transfer and fluid flow characteristics of synthetic jets." Thesis, Curtin University, 2009. http://hdl.handle.net/20.500.11937/2437.

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This thesis presents a fundamental research investigation that examines the thermal and fluid flow behaviour of a special pulsating fluid jet mechanism called synthetic jet. It is envisaged that this novel heat transfer enhancement strategy can be developed for high-performance heat sinks in electronic cooling applications.The study considers a unique arrangement of a periodic jet induced by diaphragm motion within a cavity and mounted on a confined flow channel with a heated wall upon which the jet impingement occurs. The operation of this jet mechanism is examined as two special cases for unravelling its parametric influences. In Case (a), the jet impingement is analysed in a channel with stagnant fluid permitting clear view of the pure synthetic jet process and its controlling variables. In Case (b), jet impingement is considered with fluid flow in the channel to establish the nature of synthetic jet and cross-flow interaction.The unsteady flow of this jet mechanism is simulated as a time-dependant two-dimensional numerical model with air as the working fluid. The current model considers a solution domain in its entirety, comprising the confined flow regions of the jet impinging surface, the cavity and the orifice. With a User Defined Function (UDF), the model accounts for the bulk fluid temperature variations during jet operation, which has been grossly ignored in all published work. Overcoming previous modelling limitations, the current simulation includes flow turbulence for realistic representation of pulsed jet characteristics and cross-flow interference.Computations are performed with applicable boundary conditions to obtain the heat transfer and fluid flow characteristics of the synthetic jet along with cross-flow interaction for the diaphragm amplitude ranging from 0.5 mm to 2 mm and the diaphragm frequency varying from 250 Hz to 1000 Hz. The numerical simulation yields stable solutions and aptly predicts the sequential formation of synthetic jet and its intrinsic vortex shedding process while accurately portraying the flow within the cavity.It is identified that the diaphragm amplitude primarily determines the jet velocity while the diaphragm frequency governs the rate of vortex ejection and the fluid circulation in the vicinity of the heater. The synthetic jet thermal performance is improved with high amplitude that gives rise to stronger jet impingement and reduced bulk fluid temperature arising from high frequency leading to better fluid circulation. The fluid flow in the channel or cross flow drags the jet downstream affecting jet’s ability to reach the heated wall. The relative strengths of jet velocity and channel flow determine the combined thermal performance. The fluid compressibility is seen to have insignificant effect on the synthetic jet behaviour within the examined range of parameters. As for geometrical parameters, reduced orifice width increases jet velocity improving heat transfer rates while the optima is identified for the heater -to- orifice distance within 6 to 10 times the orifice width.Results conclusively show that in a stagnant fluid medium, the proposed synthetic jet mechanism delivers 40 percent higher heat transfer rates than an equivalent continuous jet. It also thermally outperforms pure natural convection at the heated channel wall by up to 120 times within the parametric range. Under cross-flow conditions, the synthetic jet can provide 2-fold improvement in heat transfer compared to an equivalent continuous jet. By adding this synthetic jet mechanism to a flow channel, the overall thermal performance of the hybrid system is enhanced up to about 18 times the pure forced convection heat transfer rates in a channel without this jet mechanism.The observed outstanding thermal performance of the pulsed jet-cross flow hybrid mechanism surpasses the heat removal potential of current conventional techniques for electronic component cooling. It operates with a unique ability of not causing flow pressure drop increases and not requiring additional fluid circuits, which are recognised as key advantages that set this method apart from other techniques. Thus, the proposed synthetic jet-cross flow hybrid mechanism is envisaged to be potentially regarded as an outstanding thermal enhancement strategy in the development of heat sinks for future high-capacity electronic cooling needs.
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Mihic, Stefan Dragoljub. "CFD Investigation of Metalworking Fluid Flow and Heat Transfer in Grinding." University of Toledo / OhioLINK, 2011. http://rave.ohiolink.edu/etdc/view?acc_num=toledo1302189719.

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Ettrich, Jörg [Verfasser]. "Fluid Flow and Heat Transfer in Cellular Solids / Jörg Ettrich." Karlsruhe : KIT Scientific Publishing, 2014. http://www.ksp.kit.edu.

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Kent, Russell Malcolm. "Modelling fluid flow and heat transfer in some volcanic systems." Thesis, Lancaster University, 1995. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.306912.

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Книги з теми "Fluid flow and heat transfer"

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Srinivasacharya, D., and K. Srinivas Reddy, eds. Numerical Heat Transfer and Fluid Flow. Singapore: Springer Singapore, 2019. http://dx.doi.org/10.1007/978-981-13-1903-7.

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Miguel, António F., and Luiz A. O. Rocha. Tree-Shaped Fluid Flow and Heat Transfer. Cham: Springer International Publishing, 2018. http://dx.doi.org/10.1007/978-3-319-73260-2.

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

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1931-, Yang Wen-Jei, and International Symposium on Transport Phenomena (1st : 1985 : Honolulu, Hawaii), eds. Heat transfer and fluid flow in rotating machinery. Washington, D.C: Hemisphere Pub. Corp., 1987.

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Zhukauskas, A. A. Heat transfer in turbulent fluid flows. Edited by Shlanchi͡a︡uskas A and Karni J. Washington: Hemisphere Pub. Corp., 1987.

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E, Launder B., and Reece G. J. 1940-, eds. Computer-aided engineering: Heat transfer and fluid flow. Chichester, West Sussex, England: Ellis Horwood, 1985.

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A, Mosyak, and Hetsroni Gad, eds. Fluid flow, heat transfer and boiling in micro-channels. Berlin: Springer, 2009.

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Yarin, L. P. Fluid flow, heat transfer and boiling in micro-channels. Berlin: Springer, 2009.

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Owen, J. M. Flow and heat transfer in rotating-disc systems. Taunton: Research Studies, 1995.

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Owen, J. M. Flow and heat transfer in rotating-disc systems. Taunton: Research Studies Press, 1989.

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Частини книг з теми "Fluid flow and heat transfer"

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Shang, De-Yi, and Liang-Cai Zhong. "Conservation Equations of Fluid Flow." In Heat and Mass Transfer, 19–31. Cham: Springer International Publishing, 2018. http://dx.doi.org/10.1007/978-3-319-94403-6_2.

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Kleinstreuer, Clement. "Biofluid Flow and Heat Transfer." In Fluid Mechanics and Its Applications, 481–522. Dordrecht: Springer Netherlands, 2009. http://dx.doi.org/10.1007/978-1-4020-8670-0_9.

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Mobedi, Moghtada, and Gamze Gediz Ilis. "External Flow: Heat and Fluid Flow Over a Flat Plate." In Fundamentals of Heat Transfer, 103–24. Singapore: Springer Nature Singapore, 2023. http://dx.doi.org/10.1007/978-981-99-0957-5_8.

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Majumdar, Pradip. "Turbulent Flow Modeling." In Computational Fluid Dynamics and Heat Transfer, 363–94. 2nd ed. Boca Raton: CRC Press, 2021. http://dx.doi.org/10.1201/9780429183003-10.

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Faghri, Amir, and Yuwen Zhang. "Fluid-Particle Flow and Heat Transfer." In Fundamentals of Multiphase Heat Transfer and Flow, 623–86. Cham: Springer International Publishing, 2019. http://dx.doi.org/10.1007/978-3-030-22137-9_11.

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Gugulothu, Ravi, Narsimhulu Sanke, and A. V. S. S. K. S. Gupta. "Numerical Study of Heat Transfer Characteristics in Shell-and-Tube Heat Exchanger." In Numerical Heat Transfer and Fluid Flow, 375–83. Singapore: Springer Singapore, 2018. http://dx.doi.org/10.1007/978-981-13-1903-7_43.

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Pavankumar Reddy, M., and J. V. Ramana Murthy. "Heat Flow in a Rectangular Plate." In Numerical Heat Transfer and Fluid Flow, 223–31. Singapore: Springer Singapore, 2018. http://dx.doi.org/10.1007/978-981-13-1903-7_26.

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Sundén, Bengt. "Heat Transfer and Fluid Flow in Rib-Roughened Rectangular Ducts." In Heat Transfer Enhancement of Heat Exchangers, 123–40. Dordrecht: Springer Netherlands, 1999. http://dx.doi.org/10.1007/978-94-015-9159-1_8.

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Aparna, P., N. Pothanna, and J. V. Ramana Murthy. "Viscous Fluid Flow Past a Permeable Cylinder." In Numerical Heat Transfer and Fluid Flow, 285–93. Singapore: Springer Singapore, 2018. http://dx.doi.org/10.1007/978-981-13-1903-7_33.

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Joseph, Subin P. "Exact Solutions of Couple Stress Fluid Flows." In Numerical Heat Transfer and Fluid Flow, 527–35. Singapore: Springer Singapore, 2018. http://dx.doi.org/10.1007/978-981-13-1903-7_61.

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Тези доповідей конференцій з теми "Fluid flow and heat transfer"

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Narain, Amitabh, G. Yu, and Q. Liu. "COMPUTATIONAL SIMULATION AND FLOW PHYSICS FOR STRATIFIED/ANNULAR CONDENSING FLOWS." In Microgravity Fluid Physics & Heat Transfer. Connecticut: Begellhouse, 2023. http://dx.doi.org/10.1615/mfpht-1999.60.

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Ishii, Mamoru, G. Kocamustafaogullari, and Isao Kataoka. "PRESSURE AND FLUID TO FLUID SCALING LAWS FOR TWO-PHASE FLOW LOOP." In International Heat Transfer Conference 8. Connecticut: Begellhouse, 1986. http://dx.doi.org/10.1615/ihtc8.4580.

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Prasad, Bhamidi V. S. S. S., A. A. Tawfek, and A. K. Mohanty. "FLUID FLOW AND HEAT TRANSFER MEASUREMENTS FROM ROTATING CYLINDER IN CROSS FLOW." In International Heat Transfer Conference 9. Connecticut: Begellhouse, 1990. http://dx.doi.org/10.1615/ihtc9.2420.

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Guceri, Selcuk I. "Fluid Flow Problems in Processing of Composites Materials." In International Heat Transfer Conference 10. Connecticut: Begellhouse, 1994. http://dx.doi.org/10.1615/ihtc10.1960.

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Keshock, Edward G., Chin S. Lin, Patrick W. Dunn, Michael Harrison, Lawrence G. Edwards, and Joel Knapp. "PRESSURE DROP MEASUREMENTS OF TWO-PHASE FLOW IN HELICAL COILS UNDER MICROGRAVITY CONDITIONS." In Microgravity Fluid Physics & Heat Transfer. Connecticut: Begellhouse, 2023. http://dx.doi.org/10.1615/mfpht-1999.40.

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Song, Fei, Chan Y. Ching, and Dan Ewing. "Fluid flow and heat transfer modeling in rotating heat pipes." In International Heat Transfer Conference 12. Connecticut: Begellhouse, 2002. http://dx.doi.org/10.1615/ihtc12.2730.

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Muñoz-Esparza, D., J. Pérez-García, E. Sanmiguel-Rojas, A. García-Pinar, and J. P. Solano-Fernández. "Numerical simulation of incompressible laminar fluid flow in tubes with wire coil inserts." In HEAT TRANSFER 2008. Southampton, UK: WIT Press, 2008. http://dx.doi.org/10.2495/ht080051.

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Takahira, Hiroyuki, and Sanjoy Banerjee. "NUMERICAL SIMULATION OF THREE DIMENSIONAL BUBBLE GROWTH AND DETACHMENT IN A MICROGRAVITY SHEAR FLOW." In Microgravity Fluid Physics & Heat Transfer. Connecticut: Begellhouse, 2023. http://dx.doi.org/10.1615/mfpht-1999.100.

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Benedek, S. "SCALING OF TWO FLUID FLOW HEATED BY FUEL ROD." In International Heat Transfer Conference 9. Connecticut: Begellhouse, 1990. http://dx.doi.org/10.1615/ihtc9.4230.

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Borissov, Anatoly, Vladimir Shtern, Fazle Hussain, Anatoly Borissov, Vladimir Shtern, and Fazle Hussain. "Modeling flow and heat transfer in vortex burners." In 28th Fluid Dynamics Conference. Reston, Virigina: American Institute of Aeronautics and Astronautics, 1997. http://dx.doi.org/10.2514/6.1997-1998.

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Звіти організацій з теми "Fluid flow and heat transfer"

1

Juric, D., G. Tryggvason, and J. Han. Direct numerical simulations of fluid flow, heat transfer and phase changes. Office of Scientific and Technical Information (OSTI), April 1997. http://dx.doi.org/10.2172/463676.

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2

Chan, B. Improved modeling and numerics to solve two-dimensional elliptic fluid flow and heat transfer problems. Office of Scientific and Technical Information (OSTI), May 1986. http://dx.doi.org/10.2172/5579622.

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3

FRANCIS JR., NICHOLAS D., MICHAEL T. ITAMURA, STEPHEN W. WEBB, and DARRYL L. JAMES. CFD Modeling of Natural Convection Heat Transfer and Fluid Flow in Yucca Mountain Project (YMP) Enclosures. Office of Scientific and Technical Information (OSTI), March 2003. http://dx.doi.org/10.2172/809609.

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4

McHugh, P. R., and J. D. Ramshaw. A computational model for viscous fluid flow, heat transfer, and melting in in situ vitrification melt pools. Office of Scientific and Technical Information (OSTI), November 1991. http://dx.doi.org/10.2172/10140275.

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5

McHugh, P. R., and J. D. Ramshaw. A computational model for viscous fluid flow, heat transfer, and melting in in situ vitrification melt pools. Office of Scientific and Technical Information (OSTI), November 1991. http://dx.doi.org/10.2172/5504904.

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6

Pruess, K. Multiphase fluid flow and heat transfer at Hanford single-shell tanks - a progress report on modeling studies. Office of Scientific and Technical Information (OSTI), April 2000. http://dx.doi.org/10.2172/764377.

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7

Orloff, D., B. Hojjatie, and F. Bloom. High-intensity drying process: Impulse drying. Progress report on modeling of fluid flow and heat transfer in a crown compensated impulse drying roll: The heat transfer problem. Office of Scientific and Technical Information (OSTI), July 1995. http://dx.doi.org/10.2172/183137.

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8

J. Rutqvist, C.F. Tsang, and Y. Tsang. Analysis of Coupled Multiphase Fluid Flow, Heat Transfer and Mechanical Deformation at the Yucca Mountain Drift Scale Test. Office of Scientific and Technical Information (OSTI), May 2005. http://dx.doi.org/10.2172/850440.

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9

Barney, R. Hydrodynamic instabilities and heat transfer characteristics in the duct flow of a fluid in the supercritical thermodynamic regime. Office of Scientific and Technical Information (OSTI), December 2020. http://dx.doi.org/10.2172/1736328.

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10

Hammouti, A., S. Larmagnat, C. Rivard, and D. Pham Van Bang. Use of CT-scan images to build geomaterial 3D pore network representation in preparation for numerical simulations of fluid flow and heat transfer, Quebec. Natural Resources Canada/CMSS/Information Management, 2023. http://dx.doi.org/10.4095/331502.

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Анотація:
Non-intrusive techniques such as medical CT-Scan or micro-CT allow the definition of 3D connected pore networks in porous materials, such as sedimentary rocks or concrete. The definition of these networks is a key step towards the evaluation of fluid flow and heat transfer in energy resource (e.g., hydrocarbon and geothermal reservoirs) and CO2 sequestration research projects. As material heterogeneities play a role at all scales (from micro- to project-scale), numerical models represent a powerful tool for bridging the gap between small-scale measurements provided by X-ray imaging techniques and larger-scale transport properties. This study uses pre-existing medical CT-scan datasets of reference material, namely glass beads and conventional reservoir rocks (Berea sandstone, Boise sandstone, Indiana limestone) to extract the 3D geometry of connected pores using an open-source software (Spam). Pore networks from rock samples were generated from dry and then saturated samples. Binarized datasets were produced for these materials (generated by a thresholding technique) to obtain pore size distribution and tortuosity, as well as preferential paths for fluid flow. Average porosities were also calculated for comparison with those obtained by conventional commercial laboratory techniques. The results obtained show that this approach works well for medium and coarse-grained materials that do not contain a large percentage of fine particles. However, this approach does not allow representative networks to be obtained for fine-grained rocks, due to the fact that small pores (or pore throats) cannot be taken into account in the datasets obtained from the medical CT-Scan. A next step, using datasets produced from a micro- CT scan, is planned in order to be able to generate representative networks in this type of material as well.
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