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TECHNICAL PAPERS: Evaporative Boiling and Condensation

A Cavity Activation and Bubble Growth Model of the Leidenfrost Point

[+] Author and Article Information
John D. Bernardin, Issam Mudawar

Boiling and Two-Phase Flow Laboratory, School of Mechanical Engineering, Purdue University, West Lafayette, IN 47907

J. Heat Transfer 124(5), 864-874 (Sep 11, 2002) (11 pages) doi:10.1115/1.1470487 History: Received June 30, 2001; Revised January 07, 2002; Online September 11, 2002
Copyright © 2002 by ASME
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References

Bernardin,  J. D., and Mudawar,  I., 1995, “Validation of the Quench Factor Technique in Predicting Hardness in Heat Treatable Aluminum Alloys,” Int. J. Heat Mass Transf., 38, pp. 863–873.
Bernardin,  J. D., and Mudawar,  I., 1999, “The Leidenfrost Point: Experimental Study and Assessment of Existing Models,” ASME J. Heat Transfer, 121, pp. 894–903.
Clark,  H. B., Strenge,  P. S., and Westwater,  J. W., 1959, “Active Sites for Nucleate Boiling,” Chem. Eng. Prog., Symp. Ser., 55, pp. 103–110.
Gaertner,  R. F., and Westwater,  J. W., 1959, “Population of Active Sites in Nucleate Boiling Heat Transfer,” Chem. Eng. Prog., Symp. Ser., 55, pp. 39–48.
Kurihara,  H. M., and Myers,  J. E., 1960, “The Effects of Superheat and Surface Roughness on Boiling Coefficients,” AIChE J., 6, pp. 83–91.
Bankoff,  G. S., 1959, “The Prediction of Surface Temperatures at Incipient Boiling,” Chem. Eng. Prog., Symp. Ser., 55, pp. 87–94.
Hsu,  Y. Y., 1962, “On the Size Range of Active Nucleation Cavities on a Heating Surface,” ASME J. Heat Transfer, 84, pp. 207–213.
Han,  C. Y., and Griffith,  P., 1965, “The Mechanism of Heat Transfer in Nucleate Pool Boiling-Part I,” Int. J. Heat Mass Transf., 8, pp. 887–904.
Lorenz, J. J., Mikic, B. B., and Rohsenow, W. M., 1974, “The Effects of Surface Condition on Boiling,” Proc. Fifth Int. Heat Transfer Conf., 4 , Tokyo, pp. 35–39.
Gaertner,  R. F., 1965, “Photographic Study of Nucleate Pool Boiling on a Horizontal Surface,” ASME J. Heat Transfer, 87, pp. 17–29.
Cornwell, K., and Brown, R. D., 1978, “Boiling Surface Topography,” Proc. Sixth Int. Heat Transfer Conf., 1 , Toronto, Canada, pp. 157–161.
Ward, H. C., 1982, “Profile Description,” in Rough Surfaces T. R. Thomas, ed., Longman Group, New York, pp. 72–90.
Thomas, T. R., 1982, “Stylus Instruments,” in Rough Surfaces T. R. Thomas, ed., Longman Group, New York, pp. 12–70.
Brown, W. T., Jr., 1967, “Study of Flow Surface Boiling,” Ph.D. thesis, M.I.T., Cambridge, MA.
Mikic,  B. B., and Rohsenow,  W. M., 1969, “A New Correlation of Pool-Boiling Data Including the Effect of Heating Surface Characteristics,” ASME J. Heat Transfer, 91, pp. 245–250.
Bier, K., Gorenflo, D., Salem, M., and Tanes, Y., 1978, “Pool Boiling Heat Transfer and Size of Active Nucleation Centers for Horizontal Plates With Different Surface Roughness,” Proc. Sixth Int. Heat Trans. Conf., 1 , Toronto, Canada, pp. 151–156.
Yang,  S. R., and Kim,  R. H., 1988, “A Mathematical Model of the Pool Boiling Nucleation Site Density in Terms of the Surface Characteristics,” Int. J. Heat Mass Transf., 31, pp. 1127–1135.
Wang,  C. H., and Dhir,  V. K., 1993, “Effect of Surface Wettability on Active Nucleation Site Density During Pool Boiling of Water on a Vertical Surface,” ASME J. Heat Transfer, 115, pp. 659–669.
Gaertner,  R. F., 1963, “Distribution of Active Sites in the Nucleate Boiling of Liquids,” Chem. Eng. Prog., Symp. Ser., 59, pp. 52–61.
Eckert, E. R. G., and Drake, R. M., 1972, Analysis of Heat and Mass Transfer, McGraw-Hill, New York.
Panton, R. L., 1984, Incompressible Flow, John Wiley & Sons, New York.
Mikic,  B. B., Rohsenow,  W. M., and Griffith,  P., 1970, “On Bubble Growth Rates,” Int. J. Heat Mass Transf., 13, pp. 657–666.
Van Stralen,  S. J. D., Sohal,  M. S., Cole,  R., and Sluyter,  W. M., 1975, “Bubble Growth Rates in Pure and Binary Systems: Combined Effect of Relaxation and Evaporation Microlayers,” Int. J. Heat Mass Transf., 18, pp. 453–467.
Lee,  H. S., and Merte,  H., 1996, “Spherical Vapor Bubble Growth in Uniformly Superheated Liquids,” Int. J. Heat Mass Transf., 39, pp. 2427–2447.
Bankoff,  S. G., 1958, “Entrapment of Gas in the Spreading of a Liquid over a Rough Surface,” AIChE J., 4, pp. 24–26.
Bankoff,  S. G., and Mikesell,  R. D., 1959, “Bubble Growth Rates in Highly Subcooled Nucleate Boiling,” Chem. Eng. Prog., Symp. Ser., 55, pp. 95–102.
Carey, V. P., 1992, Liquid-Vapor Phase-Change Phenomena: An Introduction to the Thermophysics of Vaporization and Condensation Processes in Heat Transfer Equipment, Hemisphere, New York.
Bernardin,  J. D., Mudawar,  I., Walsh,  C. B., and Franses,  E. I., 1997, “Contact Angle Temperature Dependence for Water Droplets on Practical Aluminum Surfaces,” Int. J. Heat Mass Transf., 40, pp. 1017–1034.
Skripov, V. P., 1974, Metastable Liquids, John Wiley & Sons, New York.
Spiegler,  P., Hopenfeld,  J., Silberberg,  M., Bumpus,  C. F., and Norman,  A., 1963, “Onset of Stable Film Boiling and the Foam Limit,” Int. J. Heat Mass Transf., 6, pp. 987–994.

Figures

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Temperature dependence of vapor bubble growth for water as predicted by the numerical solution to the Rayleigh equation
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Temperature-time history of a surface during quenching in a bath of liquid
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Sessile droplet evaporation curve and corresponding photographs of water droplets approximately 2 ms after contact with a polished aluminum surface
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Depiction of (a) an actual surface profile exhibiting self-similarity and the corresponding cavity size distribution, (b) sensitivity limitation of a stylus of a surface contact profilometer, and (c) a polished aluminum surface profile (with an arithmetic average surface roughness of 26 nm) measured with a contact profilometer and the corresponding cavity size distribution
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Cavity size distributions for a polished aluminum surface determined from scanning electron microscopy images at (a) 1000×magnification, (b) 4800×magnification, and (c) combined magnifications  
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(a) Transient maximum cavity activation and bubble radius and (b) nearest-neighbor cavity distances for 25 percent cavity activation at three different times following liquid-solid contact for water on a polished aluminum surface with an interface temperature of 145°C
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Schematic representation of different forms of cavity cancellation: (a) poor vapor entrapment, (b) neighbor bubble overgrowth, and (c) bubble merging
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Transient cavity nucleation model including (a) cavity nucleation superheat criteria and corresponding cavity size distribution with transient activation window, and (b) transient maximum and minimum active cavity radii for water in contact with a hot surface with an interface temperature of 165°C
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Temperature dependence of the (a) transient vapor layer coverage and (b) average vapor layer growth rate for a sessile water droplet on a polished aluminum surface
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Average vapor layer growth rate for sessile droplets of (a) water on various polished metallic surfaces and (b) acetone, FC-72, and water on polished aluminum

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