Bibliografie tematiche / Heat transfer

Letteratura scientifica selezionata sul tema "Heat transfer"

Autore: Grafiati
Pubblicato: 4 giugno 2021
Ultima modifica: 27 luglio 2024

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Articoli di riviste sul tema "Heat transfer"

1

SARADA, Yukihiro, Ryosuke MATUMOTO e Mamoru OZAWA. "A301 HEAT TRANSFER CHARACTERISTICS OF INTERNALLY FINNED TUBE(Heat Transfer-1)". Proceedings of the International Conference on Power Engineering (ICOPE) 2009.3 (2009): _3–1_—_3–6_. http://dx.doi.org/10.1299/jsmeicope.2009.3._3-1_.

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EIAMSA-ARD, Smith, K. WONGCHAREE, S. RATTANAWONG, Petpices EIAMSA-ARD, M. PIMSARN e Chinaruk THIANPONG. "A306 TURBULENT HEAT TRANSFER THROUGH A HEAT EXCHANGER WITH POROUS TWISTED TAPE INSERTS(Heat Transfer-2)". Proceedings of the International Conference on Power Engineering (ICOPE) 2009.3 (2009): _3–31_—_3–36_. http://dx.doi.org/10.1299/jsmeicope.2009.3._3-31_.

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3

Morita, Yoshiki, e Yasuo Koizumi. "ICONE19-43109 STUDY ON BOILING HEAT TRANSFER OF MINI-HEAT TRANSFER SURFACE IN NARROW CHANNELS". Proceedings of the International Conference on Nuclear Engineering (ICONE) 2011.19 (2011): _ICONE1943. http://dx.doi.org/10.1299/jsmeicone.2011.19._icone1943_39.

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NUTHONG, Watcharin, Smith EIAMSA-ARD, Kwanchai NANAN, Petpices EIAMSA-ARD e C. THIANPONG. "A303 HEAT TRANSFER ENHANCEMENT IN A RECTANGULAR CHANNEL WITH TWISTED TAPE INSERTS(Heat Transfer-1)". Proceedings of the International Conference on Power Engineering (ICOPE) 2009.3 (2009): _3–13_—_3–17_. http://dx.doi.org/10.1299/jsmeicope.2009.3._3-13_.

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Pathak, Shriram, e Amit Kaimkuriya. "Heat Transfer Augmentation in Heat Exchanger using Nanofluid: A Review". International Journal of Trend in Scientific Research and Development Volume-2, Issue-3 (30 aprile 2018): 1939–44. http://dx.doi.org/10.31142/ijtsrd11421.

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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, n. 4 (1 aprile 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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Lochan, Rajeev, Rajeev Lochan, Hari Mohan Sharma e Deepak Agarwal. "Heat Transfer Improvement in Heat Exchanger using Porous Medium: a Review". International Journal of Innovative Research in Engineering & Management 3, n. 6 (17 novembre 2016): 468–70. http://dx.doi.org/10.21276/ijirem.2016.3.6.2.

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Alam, Irsad, e Prof Rohit Soni. "Techniques for Heat Transfer Augmentation in A Heat Exchanger: A Review". International Journal of Trend in Scientific Research and Development Volume-2, Issue-3 (30 aprile 2018): 2630–35. http://dx.doi.org/10.31142/ijtsrd12764.

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TAKEDA, Tetsuaki, e Koichi ICHIMIYA. "A305 EXPERIMENTAL STUDY ON METHOD FOR HEAT TRANSFER ENHANCEMENT USING POROUS MATERIAL WITH HIGH POROSITY(Heat Transfer-2)". Proceedings of the International Conference on Power Engineering (ICOPE) 2009.3 (2009): _3–25_—_3–30_. http://dx.doi.org/10.1299/jsmeicope.2009.3._3-25_.

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Markatos, N. C. "Heat transfer". International Journal of Heat and Mass Transfer 33, n. 5 (maggio 1990): 1039–40. http://dx.doi.org/10.1016/0017-9310(90)90088-c.

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Tesi sul tema "Heat transfer"

1

Behbahani, Reza M. "Heat transfer and heat transfer fouling in phosphoric acid evaporators". Thesis, University of Surrey, 2003. http://epubs.surrey.ac.uk/842710/.

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The primary problem in concentrating phosphoric acid is due to fouling on the tube-side of the heat exchangers of the evaporators. Scaling on the heat transfer surfaces occurs because of high supersaturation of phosphoric acid liquor with respect to calcium sulfate. A review of the existing literature reveals that no information is available on heat transfer and on crystallisation fouling of phosphoric acid solutions. Solubility of calcium sulfate is very important with regards to the scaling problems in phosphoric acid concentration plants. Hence, the solubility of different calcium sulfate types in phosphoric acid solution was studied and their dependency on acid concentration and temperature were investigated. A large number of measurements of heat transfer coefficient for water and phosphoric acid solutions under forced convective, subcooled flow boiling and pool boiling conditions at different temperatures, flow velocities, heat fluxes and concentrations were performed. The results show that the modified Gnielinski and Petukhov and Popov con-elations fit the experimental results for forced convective heat transfer to phosphoric acid solutions better than the other correlations. The Chen model and associated correlations were found suitable for the prediction of subcooled flow boiling heat transfer coefficients for phosphoric acid solutions. Applying the actual temperature driving force (Tw-Ti) instead of (Tw-Tb), a theoretical model was proposed, which permits the prediction of pool boiling heat transfer coefficients of phosphoric acid solutions with good accuracy. A large number of fouling experiments were carried out at different flow velocities, surface temperatures and concentrations to determine the mechanisms, which control deposition process. After clarification of the effect of operational parameters on the deposition process, a mathematical model was developed for prediction of fouling resistance. The activation energy evaluated for the surface reaction of the deposit formation was found to be 56,829 J/mol. The predicted fouling resistances were compared with the experimental data. Quantitative and qualitative agreement for measured and predicted fouling rates, is good. Also, a kinetic model for crystallization fouling was developed, using the field data. The predictions of the suggested model are in good agreement with the plant operating data. Finally, a numerical model was developed for computer simulation of shell and tube heat exchangers. The agreement between the field data and the prediction of the model was very satisfactory.
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Macbeth, Tyler James. "Conjugate Heat Transfer and Average Versus Variable Heat Transfer Coefficients". BYU ScholarsArchive, 2016. https://scholarsarchive.byu.edu/etd/5801.

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An average heat transfer coefficient, h_bar, is often used to solve heat transfer problems. It should be understood that this is an approximation and may provide inaccurate results, especially when the temperature field is of interest. The proper method to solve heat transfer problems is with a conjugate approach. However, there seems to be a lack of clear explanations of conjugate heat transfer in literature. The objective of this work is to provide a clear explanation of conjugate heat transfer and to determine the discrepancy in the temperature field when the interface boundary condition is approximated using h_bar compared to a local, or variable, heat transfer coefficient, h(x). Simple one-dimensional problems are presented and solved analytically using both h(x) and h_bar. Due to the one-dimensional assumption, h(x) appears in the governing equation for which the common methods to solve the differential equations with an average coefficient are no longer valid. Two methods, the integral equation and generalized Bessel methods are presented to handle the variable coefficient. The generalized Bessel method has previously only been used with homogeneous governing equations. This work extends the use of the generalized Bessel method to non-homogeneous problems by developing a relation for the Wronskian of the general solution to the generalized Bessel equation. The solution methods are applied to three problems: an external flow past a flat plate, a conjugate interface between two solids and a conjugate interface between a fluid and a solid. The main parameter that is varied is a combination of the Biot number and a geometric aspect ratio, A_1^2 = Bi*L^2/d_1^2. The Biot number is assumed small since the problems are one-dimensional and thus variation in A_1^2 is mostly due to a change in the aspect ratio. A large A_1^2 represents a long and thin solid whereas a small A_1^2 represents a short and thick solid. It is found that a larger A_1^2 leads to less problem conjugation. This means that use of h_bar has a lesser effect on the temperature field for a long and thin solid. Also, use of ¯ over h(x) tends to generally under predict the solid temperature. In addition is was found that A_2^2, the A^2 value for the second subdomain, tends to have more effect on the shape of the temperature profile of solid 1 and A_1^2 has a greater effect on the magnitude of the difference in temperature profiles between the use of h(x) and h_bar. In general increasing the A^2 values reduced conjugation.
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Roth, Eric. "Transient heat transfer". PDXScholar, 1991. https://pdxscholar.library.pdx.edu/open_access_etds/4264.

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With the advent of the new high Tc superconductors, liquid nitrogen will be one of the preferred cryogens used to cool these materials. Consequently, a more thorough understanding of the heat transfer characteristics of liquid nitrogen is required. In our investigations we examine the transient heating characteristics of liquid nitrogen to states of nucleate and film boiling under different liquid flow conditions. Using a platinum hot wire technique, it is verified that there is a premature transition to film boiling in the transient case at power levels significantly lower than under steady state nucleate boiling conditions. It is also shown that the premature transition can be reduced or eliminated depending on the flow velocity.
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Webber, Helen. "Compact heat exchanger heat transfer coefficient enhancement". Thesis, University of Bristol, 2011. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.540881.

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Riegler, Robert L. "Heat transfer optimization of grooved heat pipes /". free to MU campus, to others for purchase, 2004. http://wwwlib.umi.com/cr/mo/fullcit?p1422959.

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Wahlberg, Tobias. "Modeling of Heat Transfer". Thesis, Mälardalens högskola, Akademin för hållbar samhälls- och teknikutveckling, 2011. http://urn.kb.se/resolve?urn=urn:nbn:se:mdh:diva-12217.

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Modeling of heat transfer using Dymola. In this report a evaporator, economizer and superheater where modeled. The report describes how the models where modeled and what input was most suitable for a accurate model.
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Jones, Alastair Stephen. "Convection heat transfer problems". Thesis, Keele University, 1998. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.267356.

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Najibi, Seyed Hesam. "Heat transfer and heat transfer fouling during subcooled flow boiling for electrolyte solutions". Thesis, University of Surrey, 1997. http://epubs.surrey.ac.uk/773/.

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Holzaepfel, Gregory M. "Convective Heat Transfer in Parallel Plate Heat Sinks". Ohio University / OhioLINK, 2011. http://rave.ohiolink.edu/etdc/view?acc_num=ohiou1292521397.

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Wang, Yufei. "Heat exchanger network retrofit through heat transfer enhancement". Thesis, University of Manchester, 2012. https://www.research.manchester.ac.uk/portal/en/theses/heat-exchanger-network-retrofit-through-heat-transfer-enhancement(c504dc06-f261-4968-8c58-4f4de153c694).html.

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Abstract (sommario):
Heat exchanger network retrofit plays an important role in energy saving in process industry. Many design methods for the retrofit of heat exchanger networks have been proposed during the last three decades. Conventional retrofit methods rely heavily on topology modifications which often results in a long retrofit duration and high initial costs. Moreover, the addition of extra surface area to the heat exchanger can prove difficult due to topology, safety and downtime constraints. These problems can be avoided through the use of heat transfer enhancement in heat exchanger network retrofit. This thesis develops a heuristic methodology and an optimization methodology to consider heat transfer enhancement in heat exchanger network retrofit. The heuristic methodology is to identify the most appropriate heat exchangers requiring heat transfer enhancements in the heat exchanger network. From analysis in the heuristic roles, some great physical insights are presented. The optimisation method is based on simulated annealing. It has been developed to find the appropriate heat exchangers to be enhanced and to calculate the level of enhancement required. The new methodology allows several possible retrofit strategies using different retrofit methods be determined. Comparison of these retrofit strategies demonstrates that retrofit modification duration and pay-back time are reduced significantly when only heat transfer enhancement is utilised. Heat transfer enhancement may increase pressure drop in a heat exchanger. The fouling performance in a heat exchanger will also be affected when heat transfer enhancement is used. Therefore, the implications of pressure drop and fouling are assessed in the proposed methodology predicated on heat transfer enhancement. Methods to reduce pressure drop and mitigate fouling are developed to promote the application of heat transfer enhancement in heat exchanger network retrofit. In optimization methodology considering fouling, the dynamic nature of fouling is simulated by using temperature intervals. It can predict fouling performance when heat transfer enhancement is considered in the network. Some models for both heat exchanger and heat transfer enhancement are used to predict the pressure drop performance in heat exchanger network retrofit. Reducing pressure by modifying heat exchanger structure is proposed in this thesis. From case study, the pressure drop increased by heat transfer enhancement can be eliminated by modifying heat exchanger structure.
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Libri sul tema "Heat transfer"

1

Thomas, Lindon C. Heat transfer. London: Prentice Hall, 1992.

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2

Heat transfer. Englewood Cliffs, N.J: PTR Prentice Hall, 1993.

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Thomas, Lindon C. Heat transfer. Englewood Cliffs, N.J: Prentice-Hall, 1991.

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4

Mills, Anthony F. Heat transfer. Homewood, IL: Irwin, 1992.

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5

Heat transfer. Dubuque, Iowa: W.C. Brown, 1985.

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Wrobel, L. C., e C. A. Brebbia, a cura di. Heat Transfer. Berlin, Boston: De Gruyter, 1991. http://dx.doi.org/10.1515/9783110853209.

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Heat transfer. Dubuque, IA: McGraw-Hill, 2009.

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8

Venkateshan, S. P. Heat Transfer. Cham: Springer International Publishing, 2021. http://dx.doi.org/10.1007/978-3-030-58338-5.

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Becker, Martin. Heat Transfer. Boston, MA: Springer US, 1986. http://dx.doi.org/10.1007/978-1-4684-1256-7.

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von Böckh, Peter, e Thomas Wetzel. Heat Transfer. Berlin, Heidelberg: Springer Berlin Heidelberg, 2012. http://dx.doi.org/10.1007/978-3-642-19183-1.

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Capitoli di libri sul tema "Heat transfer"

1

Uddin, Naseem. "Heat Transfer". In Heat Transfer, 1–36. Boca Raton: CRC Press, 2023. http://dx.doi.org/10.1201/9781003428404-1.

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Becker, Martin. "Heat Exchangers". In Heat Transfer, 305–38. Boston, MA: Springer US, 1986. http://dx.doi.org/10.1007/978-1-4684-1256-7_11.

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Uddin, Naseem. "Heat Exchangers". In Heat Transfer, 447–74. Boca Raton: CRC Press, 2023. http://dx.doi.org/10.1201/9781003428404-15.

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Venkateshan, S. P. "Heat Exchangers". In Heat Transfer, 727–62. Cham: Springer International Publishing, 2021. http://dx.doi.org/10.1007/978-3-030-58338-5_15.

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von Böckh, Peter, e Thomas Wetzel. "Heat exchangers". In Heat Transfer, 215–44. Berlin, Heidelberg: Springer Berlin Heidelberg, 2011. http://dx.doi.org/10.1007/978-3-642-19183-1_8.

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Zohuri, Bahman, e Patrick McDaniel. "Heat Transfer". In Thermodynamics In Nuclear Power Plant Systems, 267–317. Cham: Springer International Publishing, 2015. http://dx.doi.org/10.1007/978-3-319-13419-2_12.

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Watson, Keith L. "Heat Transfer". In Foundation Science for Engineers, 156–66. London: Macmillan Education UK, 1993. http://dx.doi.org/10.1007/978-1-349-12450-3_17.

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Sprackling, Michael. "Heat Transfer". In Heat and Thermodynamics, 191–209. London: Macmillan Education UK, 1993. http://dx.doi.org/10.1007/978-1-349-12690-3_14.

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Sprackling, Michael. "Heat transfer". In Thermal physics, 302–36. London: Macmillan Education UK, 1991. http://dx.doi.org/10.1007/978-1-349-21377-1_18.

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Zappoli, Bernard, Daniel Beysens e Yves Garrabos. "Heat Transfer". In Heat Transfers and Related Effects in Supercritical Fluids, 125–76. Dordrecht: Springer Netherlands, 2014. http://dx.doi.org/10.1007/978-94-017-9187-8_5.

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Atti di convegni sul tema "Heat transfer"

1

Narayanaswamy, Arvind, Sheng Shen e Gang Chen. "Heat Transfer Spectroscopy and “Heat Transfer-Distance” Curves". In ASME 2008 International Mechanical Engineering Congress and Exposition. ASMEDC, 2008. http://dx.doi.org/10.1115/imece2008-69231.

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Thermal radiative transfer between objects as well as near-field forces such as van der Waals or Casimir forces have their origins in the fluctuations of the electrodynamic field. Near-field radiative transfer between two objects can be enhanced by a few order of magnitude compared to the far-field radiative transfer that can be described by Planck’s theory of blackbody radiation and Kirchoff’s laws. Despite this common origin, experimental techniques of measuring near-field forces (using the surface force apparatus and the atomic force microscope) are more sophisticated than techniques of measuring near-field radiative transfer. In this work, we present an ultra-sensitive experimental technique of measuring near-field using a bi-material atomic force microscope cantilever as the thermal sensor. Just as measurements of near-field forces results in a “force distance curve”, measurement of near-field radiative transfer results in a “heat transfer-distance” curve. Results from the measurement of near-field radiative transfer will be presented.
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2

Ryzhenkov, A. V., S. I. Pogorelov, N. A. Loginova, A. F. Mednikov e A. B. Tkhabisimov. "Radiant heat transfer reduction methods in heat insulation of power equipment". In HEAT TRANSFER 2016. Southampton UK: WIT Press, 2016. http://dx.doi.org/10.2495/ht160111.

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Kolev, N. I. "Analysis of boiling". In HEAT TRANSFER 2012. Southampton, UK: WIT Press, 2012. http://dx.doi.org/10.2495/ht120211.

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Al-Kayiem, H. H., e H. A. A. Mahdi. "Performance enhancement of rotary air preheater by the use of pin shaped turbulators". In HEAT TRANSFER 2010. Southampton, UK: WIT Press, 2010. http://dx.doi.org/10.2495/ht100041.

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Bianco, V., O. Manca e S. Nardini. "Numerical investigation of transient single phase forced convection of nanofluids in circular tubes". In HEAT TRANSFER 2008. Southampton, UK: WIT Press, 2008. http://dx.doi.org/10.2495/ht080011.

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Manca, O., S. Nardini, D. Ricci e S. Tamburrino. "Numerical investigation of natural convection of air in vertical divergent channels". In HEAT TRANSFER 2008. Southampton, UK: WIT Press, 2008. http://dx.doi.org/10.2495/ht080021.

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Selimovic, F., e B. Sundén. "Numerical simulation of fluid flow in a monolithic exchanger related to high temperature and high pressure operating conditions". In HEAT TRANSFER 2008. Southampton, UK: WIT Press, 2008. http://dx.doi.org/10.2495/ht080031.

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Boulahlib, M. S., S. Boukebbab, I. Amara e E. Ferkous. "Scalar characteristics of a lean premixed turbulent V-shape flame (air-butane)". In HEAT TRANSFER 2008. Southampton, UK: WIT Press, 2008. http://dx.doi.org/10.2495/ht080041.

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Muñoz-Esparza, D., J. Pérez-García, E. Sanmiguel-Rojas, A. García-Pinar e 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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Sousa, A. C. M., e A. Nabovati. "LBM mesoscale modelling of porous media". In HEAT TRANSFER 2008. Southampton, UK: WIT Press, 2008. http://dx.doi.org/10.2495/ht080061.

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Rapporti di organizzazioni sul tema "Heat transfer"

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Boehm, R., Y. T. Chen e A. K. Sathappan. Heat transfer studies. Office of Scientific and Technical Information (OSTI), ottobre 1995. http://dx.doi.org/10.2172/135530.

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Roth, Eric. Transient heat transfer. Portland State University Library, gennaio 2000. http://dx.doi.org/10.15760/etd.6148.

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Wynne, Nicholas Alan. HEAT TRANSFER SCOPING CALCULATIONS. Office of Scientific and Technical Information (OSTI), giugno 2019. http://dx.doi.org/10.2172/1529514.

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Stauff, Nicolas, Yinbin Miao, Sumit Bhattacharya, Yan Cao, Kan Ni e Justin Thomas. Versatile Heat Transfer Module. Office of Scientific and Technical Information (OSTI), gennaio 2022. http://dx.doi.org/10.2172/1844344.

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Shen, D. S., R. T. Mitchell, D. Dobranich, D. R. Adkins e M. R. Tuck. Micro heat spreader enhanced heat transfer in MCMs. Office of Scientific and Technical Information (OSTI), dicembre 1994. http://dx.doi.org/10.2172/10107765.

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Boehm, R., Y. T. Chen e L. Ma. Heat transfer studies. Quarterly report. Office of Scientific and Technical Information (OSTI), aprile 1995. http://dx.doi.org/10.2172/64191.

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Boehm, R., Y. T. Chen e A. K. Sathappan. Heat transfer studies, quarterly report. Office of Scientific and Technical Information (OSTI), gennaio 1996. http://dx.doi.org/10.2172/204074.

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Chow, L. C., M. Bass, J. Du, Y. Lin e T. Chung. Cryo Power and Heat Transfer. Fort Belvoir, VA: Defense Technical Information Center, settembre 2004. http://dx.doi.org/10.21236/ada430061.

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Boehm, R., Y. T. Chen e J. Vallebuona. Heat transfer studies. Quarterly report. Office of Scientific and Technical Information (OSTI), luglio 1995. http://dx.doi.org/10.2172/97299.

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Mikus, Ryan E., e Kenneth D. Kihm. Novel Heat Transfer Device Research. Fort Belvoir, VA: Defense Technical Information Center, aprile 2012. http://dx.doi.org/10.21236/ada562203.

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