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Статті в журналах з теми "Experimental methods in fluid flow, heat and mass transfer"
Krapivin, I. I., A. V. Belyaev, and A. V. Dedov. "Experimental Investigation of Boiling Heat Transfer in Freons Subjected to Forced Flow." Herald of the Bauman Moscow State Technical University. Series Natural Sciences, no. 4 (103) (August 2022): 59–79. http://dx.doi.org/10.18698/1812-3368-2022-4-59-79.
Повний текст джерелаPiasecka, Magdalena, Beata Maciejewska, and Paweł Łabędzki. "Development of FEM Calculation Methods to Analyse Subcooled Boiling Heat Transfer in Minichannels Based on Experimental Results." Applied Sciences 12, no. 24 (December 17, 2022): 12982. http://dx.doi.org/10.3390/app122412982.
Повний текст джерелаKareemullah, Mohammed, K. M. Chethan, Mohammed K. Fouzan, B. V. Darshan, Abdul Razak Kaladgi, Maruthi B. H. Prashanth, Rayid Muneer, and K. M. Yashawantha. "Heat Transfer Analysis of Shell and Tube Heat Exchanger Cooled Using Nanofluids." Recent Patents on Mechanical Engineering 12, no. 4 (December 26, 2019): 350–56. http://dx.doi.org/10.2174/2212797612666190924183251.
Повний текст джерелаAkhtar, Shehnaz, Haider Ali, and Cheol Woo Park. "Thermo-Fluidic Characteristics of Two-Phase Ice Slurry Flows Based on Comparative Numerical Methods." Processes 7, no. 12 (December 2, 2019): 898. http://dx.doi.org/10.3390/pr7120898.
Повний текст джерелаRavi, Rengarajan, and Karunakaran Rajasekaran. "Experimental study of solidification of paraffin wax in solar based triple concentric tube thermal energy storage system." Thermal Science 22, no. 2 (2018): 973–78. http://dx.doi.org/10.2298/tsci160311021r.
Повний текст джерелаWan, Junchi. "The Heat Transfer Coefficient Predictions in Engineering Applications." Journal of Physics: Conference Series 2108, no. 1 (November 1, 2021): 012022. http://dx.doi.org/10.1088/1742-6596/2108/1/012022.
Повний текст джерелаMastrullo, Rita, and Alfonso William Mauro. "Peripheral Heat Transfer Coefficient during Flow Boiling: Comparison between 2-D and 1-D Data Reduction and Discussion about Their Applicability." Energies 12, no. 23 (November 25, 2019): 4483. http://dx.doi.org/10.3390/en12234483.
Повний текст джерелаMadaliev, Murodil, Elmurad Yunusaliev, Akramjon Usmanov, Nodirakhon Usmonova, and Khusanboy Muxammadyoqubov. "Numerical study of flow around flat plate using higher-order accuracy scheme." E3S Web of Conferences 365 (2023): 01011. http://dx.doi.org/10.1051/e3sconf/202336501011.
Повний текст джерелаZhang, Yudong, Aiguo Xu, Feng Chen, Chuandong Lin, and Zon-Han Wei. "Non-equilibrium characteristics of mass and heat transfers in the slip flow." AIP Advances 12, no. 3 (March 1, 2022): 035347. http://dx.doi.org/10.1063/5.0086400.
Повний текст джерелаGopalsamy, Vijayan, Karunakaran Rajasekaran, Logesh Kamaraj, Siva Sivasaravanan, and Metin Kok. "Influence of Dimensionless Parameter on De-Ionized Water-alumina Nanofluid Based Parabolic Trough Solar Collector." Recent Patents on Nanotechnology 13, no. 3 (January 28, 2020): 206–21. http://dx.doi.org/10.2174/1872210513666190410123503.
Повний текст джерелаДисертації з теми "Experimental methods in fluid flow, heat and mass transfer"
Psimas, Michael J. "Experimental and numerical investigation of heat and mass transfer due to pulse combustor jet impingement." Diss., Georgia Institute of Technology, 2010. http://hdl.handle.net/1853/33863.
Повний текст джерела(9808835), Mohd Kabir. "Flow characteristics of Newtonian and non-Newtonian fluids in a channel with obstruction at the entry." Thesis, 2004. https://figshare.com/articles/thesis/Flow_characteristics_of_Newtonian_and_non-Newtonian_fluids_in_a_channel_with_obstruction_at_the_entry/21721064.
Повний текст джерелаThis study investigates the flow phenomena in a channel with an obstruction at the entry which is placed in another wider parallel walled channel. When obstructed, the flow phenomena inside the channel were observed to be reverse, forward or stagnant depending on the position of the obstruction. The parameters that influence the flow inside and around the test channel are: - the size and shape of the obstruction geometries, the gap between the test channel and the obstruction geometry, the Reynolds number and the length of the test channel. Knowledge of these flow phenomena has the potential benefit in the control of various flows in process engineering applications.
Experimental investigations of these flow parameters were carried out in an open channel rig. Fluids used in the investigations were a Newtonian fluid (water) and two non-Newtonian fluids, namely polyacrylamide solution (0.03% by weight) and mixed solution (xanthan gum, magna floc 139 and magna floc 1011). The polyacrylamide solution and mixed solution had similar viscosity and both show a power-law behavior, however their elastic behavior was different.
Experimental studies of these flows include the velocity measurement and the flow visualization analysis. The velocity measurement provides the quantitative information whereas flow visualization provides the qualitative information of the flow. Numerical simulations of these flow phenomena were also carried out using a CFD software and comparisons are made with the experimental results.
The influence of the size and shapes of the obstruction geometries; and the gap to width (g/w) ratio on the magnitude of the velocity ratio (ViNo: inside/outside velocity of the test channel) was studied. Obstruction geometries used were semicircle, triangle, circle and various shapes of rectangles. The g/w ratios ranging from 0.5 to 8 were selected as a set of distances from the test channel. The influence of the Reynolds numbers on the value of the velocity ratio was investigated. The effect of the test channel length on the velocity ratio was also investigated at the Reynolds number of 2000 for the above specified g/w ratios.
The flow inside the test channel was observed to be forward, reverse or stagnant for both Newtonian fluid (water) and Non-Newtonian fluids. The 'flat plate' obstruction geometry produced the maximum reverse flow inside the test channel compared with other obstruction geometries for both Newtonian and non-Newtonian fluids. The magnitude of the reverse flow for both non-Newtonian fluids used in this study is observed to be half of the magnitude of the reverse flow for water. The maximum reverse flow for non-Newtonian fluids occurs at g/w ratio of 1.0 whereas for Newtonian fluid (water) it occurs at g/w ratio of 1.5.)
The two flow parameters namely, the size and shapes of the obstruction geometries and the gap between the test channel and the obstruction geometries have the strongest influence on the flow phenomena. The Reynolds number has also a strong influence whereas the test channel length has a negligible influence on the flow phenomena.
The numerical simulations using CFD-ACE+ found that the numerically predicted streamlines and velocity vectors of the flow phenomena are in good agreement with the streak lines of the flow visualization images. It was also found that the numerical model used for this study can be generally applied for the prediction of the flow behaviour in the channel with obstruction at the entry.
(9832871), Abu Sayem. "Experimental study of electrostatic precipitator of a coal based power plant to improve performance by capturing finer particles." Thesis, 2019. https://figshare.com/articles/thesis/Experimental_study_of_electrostatic_precipitator_of_a_coal_based_power_plant_to_improve_performance_by_capturing_finer_particles/13408691.
Повний текст джерела(14042749), Shah M. E. Haque. "Performance study of the electrostatic precipitator of a coal fired power plant: Aspects of fine particulate emission control." Thesis, 2009. https://figshare.com/articles/thesis/Performance_study_of_the_electrostatic_precipitator_of_a_coal_fired_power_plant_Aspects_of_fine_particulate_emission_control/21454428.
Повний текст джерелаParticulate matter emission is one of the major air pollution problems of coal fired power plants. Fine particulates constitute a smaller fraction by weight of the total suspended particle matter in a typical particulate emission, but they are considered potentially hazardous to health because of the high probability of deposition in deeper parts of the respiratory tract. Electrostatic precipitators (ESP) are the most widely used devices that are capable of controlling particulate emission effectively from power plants and other process industries. Although the dust collection efficiency of the industrial precipitator is reported as about 99.5%, an anticipation of future stricter environmental protection agency (EPA) regulations have led the local power station seeking new technologies to achieve the new requirements at minimum cost and thus control their fine particulate emissions to a much greater degree than ever before.
This study aims to identify the options for controlling fine particle emission through improvement of the ESP performance efficiency. An ESP system consists of flow field, electrostatic field and particle dynamics. The performance of an ESP is significantly affected by its complex flow distribution arising as a result of its complex internal geometry, hence the aerodynamic characteristics of the flow inside an ESP always need considerable attention to improve the efficiency of an ESP. Therefore, a laboratory scale ESP model, geometrically similar to an industrial ESP, was designed and fabricated at the Thermodynamics Laboratory of CQUniversity, Australia to examine the flow behaviour inside the ESP. Particle size and shape morphology analyses were conducted to reveal the properties of the fly ash particles which were used for developing numerical models of the ESP.
Numerical simulations were carried out using Computational Fluid Dynamics (CFD) code FLUENT and comparisons were made with the experimental results. The ESP was modelled in two steps. Firstly, a novel 3D fluid (air) flow was modelled considering the detailed geometrical configuration inside the ESP. A novel boundary condition was applied at the inlet boundary of this model to overcome all previous assumptions on uniform velocity at the inlet boundary. Numerically predicted velocity profiles inside the ESP model are compared with the measured data obtained from the laboratory experiment. The model with a novel boundary condition predicted the flow distribution more accurately. In the second step, as the complete ESP system consists of an electric field and a particle phase in addition to the fluid flow field, a two dimensional ESP model was developed. The electrostatic force was applied to the flow equations using User Defined Functions (UDF). A discrete phase model was incorporated with this two dimensional model to study the effect of particle size, electric field and flue gas flow on the collection efficiency of particles inside the ESP. The simulated results revealed that the collection efficiency cannot be improved by the increased electric force only unless the flow velocity is optimized.
The CFD model was successfully applied to a prototype ESP at the power plant and used to recommend options for improving the efficiency of the ESP. The aerodynamic behaviour of the flow was improved by geometrical modifications in the existing 3D numerical model. In particular, the simulation was performed to improve and optimize the flow in order to achieve uniform flow and to increase particle collection inside the ESP. The particles injected in the improved flow condition were collected with higher efficiency after increasing the electrostatic force inside the 2D model. The approach adopted in this study to optimize flow and electrostatic field properties is a novel approach for improving the performance of an electrostatic precipitator.
Частини книг з теми "Experimental methods in fluid flow, heat and mass transfer"
Lu, Xianke. "Experimental Methods." In Fluid Flow and Heat Transfer in Porous Media Manufactured by a Space Holder Method, 43–80. Cham: Springer International Publishing, 2020. http://dx.doi.org/10.1007/978-3-030-53602-2_3.
Повний текст джерелаOvando Chacon, G. E., S. L. Ovando Chacon, J. C. Prince Avelino, A. Servin Martínez, and J. A. Hernández Zarate. "Numerical Simulation of the Flow in an Open Cavity with Heat and Mass Transfer." In Selected Topics of Computational and Experimental Fluid Mechanics, 357–65. Cham: Springer International Publishing, 2015. http://dx.doi.org/10.1007/978-3-319-11487-3_26.
Повний текст джерелаFiebig, M., W. Hahne, and D. Weber. "Heat Transfer and Drag Augmentation of Multiple Rows of Winglet Vortex Generators in Transitional Channel Flow: A Comparison of Numerical and Experimental Methods." In Notes on Numerical Fluid Mechanics (NNFM), 88–94. Wiesbaden: Vieweg+Teubner Verlag, 1996. http://dx.doi.org/10.1007/978-3-322-89838-8_12.
Повний текст джерелаHaidn, Oskar J., Nikolaus A. Adams, Rolf Radespiel, Thomas Sattelmayer, Wolfgang Schröder, Christian Stemmer, and Bernhard Weigand. "Collaborative Research for Future Space Transportation Systems." In Notes on Numerical Fluid Mechanics and Multidisciplinary Design, 1–30. Cham: Springer International Publishing, 2020. http://dx.doi.org/10.1007/978-3-030-53847-7_1.
Повний текст джерелаHan, Je-Chin, and Lesley M. Wright. "Mass Transfer Analogy Measurement Techniques." In Experimental Methods in Heat Transfer and Fluid Mechanics, 263–85. CRC Press, 2020. http://dx.doi.org/10.1201/9781003021179-10.
Повний текст джерелаHan, Je-Chin, and Lesley M. Wright. "Velocity and Flow Rate Measurements." In Experimental Methods in Heat Transfer and Fluid Mechanics, 17–40. CRC Press, 2020. http://dx.doi.org/10.1201/9781003021179-2.
Повний текст джерелаHan, Je-Chin, and Lesley M. Wright. "Flow and Thermal Field Measurement Techniques." In Experimental Methods in Heat Transfer and Fluid Mechanics, 287–327. CRC Press, 2020. http://dx.doi.org/10.1201/9781003021179-11.
Повний текст джерелаHan, Je-Chin, and Lesley M. Wright. "Flow Field Measurements by Particle Image Velocimetry (PIV) Techniques." In Experimental Methods in Heat Transfer and Fluid Mechanics, 329–63. CRC Press, 2020. http://dx.doi.org/10.1201/9781003021179-12.
Повний текст джерелаVajravelu, Kuppalapalle, and Swati Mukhopadhyay. "Numerical methods." In Fluid Flow, Heat and Mass Transfer At Bodies of Different Shapes, 3–6. Elsevier, 2016. http://dx.doi.org/10.1016/b978-0-12-803733-1.00001-6.
Повний текст джерелаMasuda, Hayato. "Enhancement of Heat Transfer Using Taylor Vortices in Thermal Processing for Food Process Intensification." In Food Processing – New Insights [Working Title]. IntechOpen, 2021. http://dx.doi.org/10.5772/intechopen.99443.
Повний текст джерелаТези доповідей конференцій з теми "Experimental methods in fluid flow, heat and mass transfer"
Tibiric¸a´, Cristiano Bigonha, and Gherhardt Ribatski. "Experimental Investigation of Flow Boiling Pressure Drop of R134a in a Micro-Scale Horizontal Smooth Tube." In 2010 14th International Heat Transfer Conference. ASMEDC, 2010. http://dx.doi.org/10.1115/ihtc14-22962.
Повний текст джерелаBachert, B., M. Dular, S. Baumgarten, G. Ludwig, and B. Stoffel. "Experimental Investigations Concerning Erosive Aggressiveness of Cavitation at Different Test Configurations." In ASME 2004 Heat Transfer/Fluids Engineering Summer Conference. ASMEDC, 2004. http://dx.doi.org/10.1115/ht-fed2004-56597.
Повний текст джерелаBakhtiyarov, Sayavur I., and Ruel A. Overfelt. "Numerical Simulation and Experimental Study of Heat and Mass Transfer Phenomena in Vacuum-Sealed Casting Process." In ASME 2002 Joint U.S.-European Fluids Engineering Division Conference. ASMEDC, 2002. http://dx.doi.org/10.1115/fedsm2002-31122.
Повний текст джерелаMolchanov, Alexander M., and Anna A. Arsentyeva. "Numerical Simulation of Heat Transfer and Fluid Dynamics in Supersonic Chemically Reacting Flows." In 2010 14th International Heat Transfer Conference. ASMEDC, 2010. http://dx.doi.org/10.1115/ihtc14-22371.
Повний текст джерелаSˇaric´, Sanjin, Suad Jakirlic´, and Cameron Tropea. "A Periodically Perturbed Backward-Facing Step Flow by Means of LES, DES and T-RANS: An Example of Flow Separation Control." In ASME 2004 Heat Transfer/Fluids Engineering Summer Conference. ASMEDC, 2004. http://dx.doi.org/10.1115/ht-fed2004-56514.
Повний текст джерелаChaquet, Jose M., Roque Corral, Guillermo Pastor, Jesus Pueblas, and D. D. Coren. "Validation of a Coupled Fluid/Solid Heat Transfer Method." In ASME 2011 Turbo Expo: Turbine Technical Conference and Exposition. ASMEDC, 2011. http://dx.doi.org/10.1115/gt2011-45951.
Повний текст джерелаMa, Tengxiao, and Leping Zhou. "Fluid Flow and Thin Film Evolution Near the Triple Line of Evaporative Sessile Droplet During Mixing Process." In ASME 2019 6th International Conference on Micro/Nanoscale Heat and Mass Transfer. American Society of Mechanical Engineers, 2019. http://dx.doi.org/10.1115/mnhmt2019-4085.
Повний текст джерелаWilliams, K. A., D. M. Snider, J. R. Torczynski, S. M. Trujillo, and T. J. O’Hern. "Multiphase Particle-in-Cell Simulations of Flow in a Gas-Solid Riser." In ASME 2004 Heat Transfer/Fluids Engineering Summer Conference. ASMEDC, 2004. http://dx.doi.org/10.1115/ht-fed2004-56594.
Повний текст джерелаSadikin, Azmahani, David A. McNeil, and Khalid H. Barmadouf. "Two-Phase Flow on the Shell Side of a Shell and Tube Heat Exchanger." In 2010 14th International Heat Transfer Conference. ASMEDC, 2010. http://dx.doi.org/10.1115/ihtc14-22790.
Повний текст джерелаMinchola, L. R., L. F. A. Azevedo, and A. O. Nieckele. "The Influence of Rheological Parameters in Wax Deposition in Channel Flow." In 2010 14th International Heat Transfer Conference. ASMEDC, 2010. http://dx.doi.org/10.1115/ihtc14-22952.
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