Abstract
A key challenge in the design of efficient energy conversion systems is to achieve effective heat transfer at temperatures that can extract the maximum thermodynamic potential of the system’s heat source. In classical heat exchangers, heat transfer takes place through a wall separating the hot and the cold fluid streams. Thus, conventional heat exchangers are limited in their ability to tap the maximum thermodynamic potential because they have built-in thermal losses associated with the separation of the fluid streams by an intervening solid wall. This type of configuration also leads to a deterioration of the heat transfer effectiveness as the heat transfer coefficients decrease with time due to fouling. In the case of high-temperature applications, thermal stress and corrosion problems are imposed on the wall materials themselves. These situations are present irrespective of whether the two fluid streams are solid, liquid, vapor, gaseous, or some mixtures of them.
Access this chapter
Tax calculation will be finalised at checkout
Purchases are for personal use only
Preview
Unable to display preview. Download preview PDF.
References
Borodulya, V. A., and Kovensky, V. I., (1983), “Radiative Heat Transfer Between a Fluidized Bed and a Surface,” Int. J. Heat Mass Transfer, Vol. 26, No. 2, pp. 277–287.
Chan, C. K., and Tien, C. L., (1974), “Radiative Transfer in Packed Spheres,” Trans. ASME Ser. C, Vol. 96, p. 52.
Epstein, N. (1984), “Hydrodynamics of Three-Phase Fluidization,” Chapter 23 in Handbook of Fluids in Motion, Ann Arbor Science.
Fair, J. R. (1972), “Designing Direct-Contact Coolers/Condensers,” Chemical Engineering, June 12, pp. 91-100.
Flamant, G. (1982), “Theoretical and Experimental Study of Radiant Heat Transfer in a Solar Fluidized-Bed Receiver,” AIChE Journal, Vol. 28, No. 4, pp. 529–535.
Jacobs, H., and R. Boehm (1980), “Direct-Contact Binary Cycles,” Section 4.2.6 in Source book on the Production of Electricity From Geothermal Energy (J. Kestin et al., Eds.), U.S. Department of Energy, Report DOE/RA/4051-1, pp. 413-471.
Rohsenow, W., J. Harnett, E. Ganic, eds. (1985), Chapter 10, Handbook of Heat Transfer Applications, McGraw-Hill, New York.
Saxena, S. C, and Gabor, J. D. (1981), “Mechanisms of Heat Transfer Between a Surface and a Gas-Fluidized Bed for Combustor Applications,” Prog. Energy Combust. Sci., Vol. 7, pp. 73–102.
Saxena, S., N. Grewal, J. Gabor, S. Zabrodsky, and D. Galershtein (1981), “Heat Transfer Between a Gas-Fluidized Bed and Immersed Tubes,” in Advances in Heat Transfer, Vol. 14.
Sideman, S. (1966), “Direct-Contact Heat Transfer Between Immiscible Liquids,” in Advances in Chemical Engineering, Vol. 6, pp. 207–286.
Sideman, S., and Y. Gat (1966), “Direct-Contact Heat Transfer with Change of Phase: Spray-Column Studies of a Three-Phase Heat Exchanger,” AIChE Journal, March, pp. 296-303.
Sideman, S., and D. Moalem-Maron (1982), “Direct-Contact Condensation,” in Advances in Heat Transfer, Vol. 15, pp. 227–281.
Vallario, R., and D. DeBellis (1984), “State of Technology of Direct-Contact Heat Exchanging,” Pacific Northwest Laboratory, Report PNL-5009, UC-95, May.
Zabrodsky, S. (1966), Hydrodynamics and Heat Transfer in Fluidized Beds, MIT Press.
Editor information
Editors and Affiliations
Rights and permissions
Copyright information
© 1988 Springer-Verlag Berlin Heidelberg
About this paper
Cite this paper
Boehm, R.F., Kreith, F. (1988). Direct-Contact Heat Transfer Processes. In: Kreith, F., Boehm, R.F. (eds) Direct-Contact Heat Transfer. Springer, Berlin, Heidelberg. https://doi.org/10.1007/978-3-662-30182-1_1
Download citation
DOI: https://doi.org/10.1007/978-3-662-30182-1_1
Publisher Name: Springer, Berlin, Heidelberg
Print ISBN: 978-3-662-30184-5
Online ISBN: 978-3-662-30182-1
eBook Packages: Springer Book Archive