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Добірка наукової літератури з теми "Heat flows"

Автор: Grafiati

Опубліковано: 13 липня 2022

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Статті в журналах з теми "Heat flows"

1

Gorin, Alexander V. "HEAT TRANSFER IN TURBULENT SEPARATED FLOWS(Flow around Cylinder 1)." Proceedings of the International Conference on Jets, Wakes and Separated Flows (ICJWSF) 2005 (2005): 445–50. http://dx.doi.org/10.1299/jsmeicjwsf.2005.445.

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2

Adamovský, D., P. Neuberger, D. Herák, and R. Adamovský. "Exergy of heat flows in exchanger consisting f gravity heat pipes." Research in Agricultural Engineering 51, No. 3 (February 7, 2012): 73–78. http://dx.doi.org/10.17221/4906-rae.

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The paper deals with the analysis of the impact of inlet air temperature on the exergy efficiency and exergy of the losing heat flow and determination of the relation between the exergy and thermal efficiency in an exchanger consisting of gravity heat pipes. The assessment of heat processes quality and transformation of energy in the exchanger are also dealt with.

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3

Adamovský, R., D. Adamovský, and D. Herák. "Exergy of heat flows of the air-to-air plate heat exchanger." Research in Agricultural Engineering 50, No. 4 (February 8, 2012): 130–35. http://dx.doi.org/10.17221/4939-rae.

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Based on extensive measurements of the temperature, humidity and flow rate of the heated and cooled air in the plate heat exchanger this article analyses the influence of air inlet temperatures on both the exergy efficiency of the heat exchanger and the heat loss exergy. Furthermore, it describes the dependence between the thermal and exergy efficiency of the heat exchanger. The analysis of the tested heat exchanger indicated that the exergy efficiency of heat utilization from cooled air increases with rising inlet air temperature different, while the exergy efficiency of the heat transfer from cool to heated air decreases. In addition, the experiments confirmed the validity of the relationship between heat loss exergy and the values of air inlet temperatures.

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4

Cheng, Ping, and T. S. Zhao. "HEAT TRANSFER IN OSCILLATORY FLOWS." Annual Review of Heat Transfer 9, no. 9 (1998): 359–420. http://dx.doi.org/10.1615/annualrevheattransfer.v9.90.

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5

Lemm, Marius, and Vladimir Markovic. "Heat flows on hyperbolic spaces." Journal of Differential Geometry 108, no. 3 (March 2018): 495–529. http://dx.doi.org/10.4310/jdg/1519959624.

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6

Evans, L. C., O. Savin, and W. Gangbo. "Diffeomorphisms and Nonlinear Heat Flows." SIAM Journal on Mathematical Analysis 37, no. 3 (January 2005): 737–51. http://dx.doi.org/10.1137/04061386x.

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7

Takamura, S., M. Y. Ye, T. Kuwabara, and N. Ohno. "Heat flows through plasma sheaths." Physics of Plasmas 5, no. 5 (May 1998): 2151–58. http://dx.doi.org/10.1063/1.872888.

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8

Bregman, Joel N., and L. P. David. "Heat conduction in cooling flows." Astrophysical Journal 326 (March 1988): 639. http://dx.doi.org/10.1086/166122.

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9

Michaelides, Efstathios E. "Heat transfer in particulate flows." International Journal of Heat and Mass Transfer 29, no. 2 (February 1986): 265–73. http://dx.doi.org/10.1016/0017-9310(86)90233-4.

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10

Khalatov, A. A. "Heat transfer in swirled flows." Journal of Engineering Physics and Thermophysics 64, no. 6 (June 1993): 546–51. http://dx.doi.org/10.1007/bf01089954.

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Дисертації з теми "Heat flows"

1

Takamura, S., M. Y. Ye, T. Kuwabara, and N. Ohno. "Heat flows through plasma sheaths." American Institute of Physics, 1998. http://hdl.handle.net/2237/6995.

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2

Astin, P. "Heat transfer in jet assimilation flows." Thesis, Keele University, 1990. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.292751.

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3

Amin, Norsarahaida. "Oscillation-induced mean flows and heat transfer." Thesis, University of East Anglia, 1989. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.329339.

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4

Shu, Jian-Jun. "Heat characteristics of some thin film flows." Thesis, Keele University, 1991. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.314615.

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5

Li, Jintang. "Heat transfer in gas-solids flows through pipes." Thesis, Glasgow Caledonian University, 2000. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.313180.

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6

Mankad, Sunil. "Heat transfer in two phase solid-liquid flows." Thesis, University of Cambridge, 1995. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.307988.

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7

Tait, Nicole Lynn. "Recovery factors in zero-mean internal oscillatory flows." Thesis, Monterey, Calif. : Springfield, Va. : Naval Postgraduate School ; Available from National Technical Information Service, 1995. http://handle.dtic.mil/100.2/ADA306233.

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Thesis (M.S. in Mechanical Engineering and M.S. in Astronautical Engineering) Naval Postgraduate School, December 1995.
"December 1995." Thesis advisor(s): Ashok Gopinath, Oscar Biblarz. Bibliography: p. 61. Also available online.

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8

Moore, Bryce Kirk. "Gas-liquid flows in adsorbent microchannels." Thesis, Georgia Institute of Technology, 2013. http://hdl.handle.net/1853/47519.

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A study of two the sequential displacement of gas and liquid phases in microchannels for eventual application in temperature swing adsorption (TSA) methane purification systems was performed. A model for bulk fluid displacement in 200 m channels was developed and validated using data from an air-water flow visualization study performed on glass microchannel test sections with a hydraulic diameter of 203 m. High-speed video recording was used to observe displacement samples at two separate channel locations for both the displacement of gas by liquid and liquid by gas, and for driving pressure gradients ranging from 19 to 450 kPa m-1. Interface velocities, void fractions, and film thicknesses were determined using image analysis software for each of the 63 sample videos obtained. Coupled 2-D heat and mass transfer models were developed to simulate a TSA gas separation process in which impurities in the gas supply were removed through adsorption into adsorbent coated microchannel walls. These models were used to evaluate the impact of residual liquid films on system mass transfer during the adsorption process. It was determined that for a TSA methane purification system to be effective, it is necessary to purge liquid from the adsorbent channel. This intermediate purge phase will benefit the mass transfer performance of the adsorption system by removing significant amounts of residual liquid from the channel and by causing the onset of rivulet flow in the channel. The existence of the remaining dry wall area, which is characteristic of the rivulet flow regime, improves system mass transfer performance in the presence of residual liquid. The commercial viability of microchannel TSA gas separation systems depends strongly on the ability to mitigate the presence and effects of residual liquid in the adsorbent channels. While the use of liquid heat transfer fluids in the microchannel structure provides rapid heating and cooling of the adsorbent mass, the management of residual liquid remains a significant hurdle. In addition, such systems will require reliable prevention of interaction between the adsorbent and the liquid heat transfer fluid, whether through the development and fabrication of highly selective polymer matrix materials or the use of non-interacting large-molecule liquid heat transfer fluids. If these hurdles can be successfully addressed, microchannel TSA systems may have the potential to become a competitive technology in large-scale gas separation.

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9

Seyedein, Seyed Hossein. "Simulation of fluid flow and heat transfer in impingement flows of various configurations." Thesis, McGill University, 1993. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=69587.

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Results of numerical simulation of two-dimensional flow field and heat transfer impingement due to laminar and turbulent single as well as multiple slot jets discharging normally into a confined channel are presented. Both low-Reynolds and high-Reynolds number versions of $k - epsilon$ models were used to model the turbulent jet flow. A control volume-based finite difference method was employed to solve the governing mass, momentum, turbulent kinetic energy, turbulent kinetic energy dissipation rate and energy equations in the turbulent impinging jet cases. A separate program was written based on a body-fitted coordinate system to predict the transport characteristics of multiple laminar jets impinging on a plate surface with an inclined upper confinement surface. The parameters studied include: the jet Reynolds number, nozzle-to-impingement surface spacing and for the inclined confinement surface cases, the angle of inclination of the upper surface. From the low-Reynolds number model studied it was found that models presented by Lam-Bremhorst and Launder-Sharma to be applicable to single turbulent jet impingement heat transfer predictions. Inclination of the confined surface so as to accelerate the exhaust flow was found to level the Nusselt number distribution on the impingement surface.

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10

Huang, Tao. "REGULARITY AND UNIQUENESS OF SOME GEOMETRIC HEAT FLOWS AND IT'S APPLICATIONS." UKnowledge, 2013. http://uknowledge.uky.edu/math_etds/10.

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This manuscript demonstrates the regularity and uniqueness of some geometric heat flows with critical nonlinearity. First, under the assumption of smallness of renormalized energy, several issues of the regularity and uniqueness of heat flow of harmonic maps into a unit sphere or a compact Riemannian homogeneous manifold without boundary are established. For a class of heat flow of harmonic maps to any compact Riemannian manifold without boundary, satisfying the Serrin's condition, the regularity and uniqueness is also established. As an application, the hydrodynamic flow of nematic liquid crystals in Serrin's class is proved to be regular and unique. The natural extension of all the results to the heat flow of biharmonic maps is also presented in this manuscript.

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Книги з теми "Heat flows"

1

Yeoh, Guan Heng. Modelling subcooled boiling flows. New York: Nova Science Publishers, 2008.

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2

Pedišius, A. Heat transfer augmentation in turbulent flows. Kaunas: Lithuanian Energy Institute, 1995.

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3

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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4

Terekhov, Viktor I., Aleksey Yu Dyachenko, Yaroslav J. Smulsky, Tatyana V. Bogatko, and Nadezhda I. Yarygina. Heat Transfer in Subsonic Separated Flows. Cham: Springer International Publishing, 2022. http://dx.doi.org/10.1007/978-3-030-94557-2.

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5

Lidia, Palese, ed. Stability criteria for fluid flows. New Jersey: World Scientific, 2009.

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6

Georgescu, Adelina. Stability criteria for fluid flows. New Jersey: World Scientific, 2009.

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7

Amin, Norsarahaida. Oscillation-induced mean flows and heat transfer. Norwich: University of East Anglia, 1989.

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8

A, Mikhaĭlov I͡U︡, and Ozols R. 1941-, eds. Heat and mass transfer in MHD flows. Singapore: World Scientific, 1987.

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9

Shang, De-Yi. Free Convection Film Flows and Heat Transfer. Berlin, Heidelberg: Springer Berlin Heidelberg, 2012. http://dx.doi.org/10.1007/978-3-642-28983-5.

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10

Nagabushana, K. A. Heat transfer from cylinders in subsonic slip flows. Hampton, Va: Langley Research Center, 1992.

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Частини книг з теми "Heat flows"

1

Cebeci, Tuncer. "Buoyant Flows." In Convective Heat Transfer, 101–7. Berlin, Heidelberg: Springer Berlin Heidelberg, 2002. http://dx.doi.org/10.1007/978-3-662-06406-1_8.

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2

Mauri, Roberto. "Heat Conduction." In Transport Phenomena in Multiphase Flows, 155–73. Cham: Springer International Publishing, 2015. http://dx.doi.org/10.1007/978-3-319-15793-1_9.

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3

Cebeci, Tuncer. "Laminar Duct Flows." In Convective Heat Transfer, 53–70. Berlin, Heidelberg: Springer Berlin Heidelberg, 2002. http://dx.doi.org/10.1007/978-3-662-06406-1_5.

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4

Cebeci, Tuncer. "Turbulent Duct Flows." In Convective Heat Transfer, 87–99. Berlin, Heidelberg: Springer Berlin Heidelberg, 2002. http://dx.doi.org/10.1007/978-3-662-06406-1_7.

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5

Sidebotham, George. "Internal Flows Models." In Heat Transfer Modeling, 405–43. Cham: Springer International Publishing, 2015. http://dx.doi.org/10.1007/978-3-319-14514-3_11.

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6

Naterer, Greg F. "Chemically Reacting Flows." In Advanced Heat Transfer, 355–98. 3rd ed. Boca Raton: CRC Press, 2021. http://dx.doi.org/10.1201/9781003206125-8.

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7

Mauri, Roberto. "Convective Heat Transport." In Transport Phenomena in Multiphase Flows, 221–33. Cham: Springer International Publishing, 2015. http://dx.doi.org/10.1007/978-3-319-15793-1_13.

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8

Mauri, Roberto. "Radiant Heat Transfer." In Transport Phenomena in Multiphase Flows, 339–52. Cham: Springer International Publishing, 2015. http://dx.doi.org/10.1007/978-3-319-15793-1_20.

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9

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

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10

Mauri, Roberto. "Conduction with Heat Sources." In Transport Phenomena in Multiphase Flows, 175–89. Cham: Springer International Publishing, 2015. http://dx.doi.org/10.1007/978-3-319-15793-1_10.

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Тези доповідей конференцій з теми "Heat flows"

1

Abraham, J. P., E. M. Sparrow, J. C. K. Tong, and W. J. Minkowycz. "Intermittent Flow Modeling: Part 2—Time-Varying Flows and Flows in Variable Area Ducts." In 2010 14th International Heat Transfer Conference. ASMEDC, 2010. http://dx.doi.org/10.1115/ihtc14-22696.

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The all-flow-regime model of fluid flow, previously applied in [1] to flows with axially and temporally uniform Reynolds numbers, has been implemented here for flows in which the Reynolds number may either vary with time or along the length of a pipe. In the former situation, the timewise variations were driven by a harmonically oscillating inlet flow. These oscillations created a succession of flow-regime transitions encompassing purely laminar and purely turbulent flows as well as laminarizing and turbulentizing flows where intermittency prevailed. The period of the oscillations was increased parametrically until the quasi-steady regime was attained. The predicted quasi-steady friction factors were found to be in excellent agreement with those from a simple model under which the flow is assumed to pass through a sequence of instantaneous steady states. In the second category of non-constant-Reynolds-number flows, axial variations of a steady flow were created by means of a finite-length conical enlargement which connected a pair of pipes of constant but different diameters. The presence of the cross-sectional enlargement gives rise to a reduction of the Reynolds number that is proportional to the ratio of the diameters of the upstream and the downstream pipes. Depending on the magnitude of the upstream inlet Reynolds number, the downstream fully developed flow could variously be laminar, intermittent, or turbulent. The presence or absence of flow separation in the conical enlargement had a direct effect on the laminarization process. For both categories of non-constant-Reynolds-number flows, laminarization and turbulentization were quantified by the ratio of the rate of turbulence production to the rate of turbulence destruction.

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2

Nobile, Enrico, Antonio C. M. Sousa, and Giovanni S. Barozzi. "TURBULENT BUOYANT FLOWS IN ENCLOSURES." In International Heat Transfer Conference 9. Connecticut: Begellhouse, 1990. http://dx.doi.org/10.1615/ihtc9.3280.

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3

Hunt, M. L., and S. S. Hsiau. "THERMAL CONDUCTIVITY OF GRANULAR FLOWS." In International Heat Transfer Conference 9. Connecticut: Begellhouse, 1990. http://dx.doi.org/10.1615/ihtc9.3420.

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4

Oosthuizen, Patrick H. "Some Complex Natural Convective Flows." In International Heat Transfer Conference 12. Connecticut: Begellhouse, 2002. http://dx.doi.org/10.1615/ihtc12.3270.

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5

Narayanan, V. "Time-Resolved Thermal Surface Flow Structures in Impinging Slot Jet Flows." In ASME 2003 Heat Transfer Summer Conference. ASMEDC, 2003. http://dx.doi.org/10.1115/ht2003-47493.

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Анотація:

This paper presents low-frequency time-resolved measurements of impingement surface temperature in a turbulent submerged impinging slot jet flow at an exit Reynolds number of 22,500 using infrared (IR) thermography. The nozzle-to-surface spacing was varied from 0.5 to 5 nozzle hydraulic diameters. Time-traces of temperature at specific locations of interest, identified from mean temperature maps, are presented. At a nozzle spacing of 5 hydraulic diameters corresponding to transitional jet impingement, the time traces of surface temperature show mild, but periodically repeating hot and cold streaks, suggesting the presence of near-wall streamwise counter-rotating vortex pairs along the impingement line. At a closer nozzle spacing of 0.5 hydraulic diameter corresponding to impingement of the jet potential core, the temperature streaks at the impingement line could not be detected. Previously unreported distinct thermal streaks are observed at locations corresponding to the local minimum and secondary maximum in heat transfer. Data of rms-averaged temperature fluctuations for the two spacings corroborate well with time trace observations.

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6

Campbell, Charles S., and David G. Wang. "Effective Conductivity of Shearing Particle Flows." In International Heat Transfer Conference 8. Connecticut: Begellhouse, 1986. http://dx.doi.org/10.1615/ihtc8.3700.

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7

Peters, Wayne D., James E. S. Venart, and Charles R. Dutcher. "GRAVITY CURRENT FLOWS OVER ROUGH SURFACES." In International Heat Transfer Conference 10. Connecticut: Begellhouse, 1994. http://dx.doi.org/10.1615/ihtc10.3130.

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8

Deodat Makhanlall. "HEAD LOSSES IN DUCT FLOWS WITH CONDUCTION-RADIATION HEAT TRANSFER." In 23rd ABCM International Congress of Mechanical Engineering. Rio de Janeiro, Brazil: ABCM Brazilian Society of Mechanical Sciences and Engineering, 2015. http://dx.doi.org/10.20906/cps/cob-2015-2641.

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9

Sapiro, Guillermo, and Allen R. Tannenbaum. "Formulating invariant heat-type curve flows." In SPIE's 1993 International Symposium on Optics, Imaging, and Instrumentation, edited by Baba C. Vemuri. SPIE, 1993. http://dx.doi.org/10.1117/12.146629.

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10

Ogino, Fumimaru. "TURBULENT TRANSPORT PHENOMENA IN THERMALLY STRATIFIED FLOWS." In International Heat Transfer Conference 9. Connecticut: Begellhouse, 1990. http://dx.doi.org/10.1615/ihtc9.2190.

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Звіти організацій з теми "Heat flows"

1

Richard J. Goldstein. Heat Transfer Enhancement in Separated and Vortex Flows. Office of Scientific and Technical Information (OSTI), May 2004. http://dx.doi.org/10.2172/825973.

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2

Thompson, C. Stability and heat transfer in time-modulated flows. Office of Scientific and Technical Information (OSTI), January 1991. http://dx.doi.org/10.2172/5933652.

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3

Thompson, C. Stability and heat transfer in time-modulated flows. Office of Scientific and Technical Information (OSTI), January 1992. http://dx.doi.org/10.2172/6835979.

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4

Campbell, C. S. Mechanics/heat-transfer relation for particle flows: Quarterly report. Office of Scientific and Technical Information (OSTI), January 1989. http://dx.doi.org/10.2172/6233102.

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5

Thompson, C. Stability and heat transfer in time-modulated flows. Final report. Office of Scientific and Technical Information (OSTI), January 1998. http://dx.doi.org/10.2172/564318.

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6

Pasinato, Hugo D. Computation and Modeling of Heat Transfer in Wall-Bounded Turbulent Flows. Fort Belvoir, VA: Defense Technical Information Center, May 2010. http://dx.doi.org/10.21236/ada563677.

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7

Taborek, Peter. Nanoscale Heat Transfer Due to Near Field Radiation and Nanofluidic Flows. Fort Belvoir, VA: Defense Technical Information Center, July 2015. http://dx.doi.org/10.21236/ada625941.

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8

Thompson, C. Stability and heat transfer in time-modulated flows. Technical progress report. Office of Scientific and Technical Information (OSTI), December 1992. http://dx.doi.org/10.2172/10113906.

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9

Zeng, Y., H. Yu, and X. Wang. Relationship Between Heat Flows and Geological Structures in the Sichuan Basin, P.R. China. Office of Scientific and Technical Information (OSTI), January 1995. http://dx.doi.org/10.2172/895939.

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10

Alexander, Aaron, Luc Mongeau, and James E. Braun. Performance of Straight-Fin and Microchannel Heat Exchangers in Steady and Periodic Flows. Fort Belvoir, VA: Defense Technical Information Center, October 2001. http://dx.doi.org/10.21236/ada390420.

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