Références

Reférences

[1] JENS, W.H., AND LOTTES, P. A. Analysis of heat transfer burnout, pressure drop, and density data for high-pressure water. Tech. rep., Argonne National Laboratories, 1951

[2]Thom, J. R. S., Walker, W. M., Fallon, T. A., and Reising, G. F. S. Boiling in subcooled water during flow up heated tubes or annuli. In Symposium on Boiling Heat Transfer in Steam Generating Units and Heat Exchangers (Institute of Mechanical Engineers,London, 1965)

[3]Chen, J. C. A correlation for boiling heat transfer for satured fluids in convective flows. Industrial and Engineering Chemistry Process Design and Development 5 (1966), 322–329

[4] Gungor, K. E., and Winterton, R. H. S. A general correlation for flow boiling in tubes and annuli. International Journal of Heat and Mass Transfer 29, 3 (1986), 351–358

[5] Liu, Z., and Winterton, R. H. S. A general correlation for saturated and subcooledflow boiling in tubes and annuli, based on a nucleate pool boiling equation. International Journal of Heat and Mass Transfer 34, 11 (1991), 2759–2766.

[6] Kurul, N., and Podowski, M. Multidimensional effects in forced convection subcooled boiling. In Proceedings of the 9th Heat Transfer Conference (1990), pp. 21–26.

[7] Dittus, F. W., and Boelter, L. M. K. Heat transfer in automobile radiators of the tubular type. University of California Publications on Engineering, Berkeley, California 2,13 (1930), 443–461.

[8] Lemmert, M., and Chwala, J. M. Influence of flow velocity on surface boiling heat transfer coefficient. Heat Transfer in Boiling (1977), 237–247

[9] Ceumern-Lindenstjerna, W. C. Bubble departure diameter and release frequencies during nucleate pool boiling of water and aqueous nacl solutions. Heat Transfer in boiling (1977).

[10] Yeoh, G. H., and Tu, J. Y. A unified model considering force balances for departing vapour bubbles and population balance in subcooled boiling flow. Nuclear Engineering and Design 235 (2005), 1251–1265.

[11] Judd, R. L., and Hwang, K. S. A comprehensive model for nucleate pool boiling heat transfer including microlayer evaporation. Journal of Heat Transfer (1976), 623–629

[12] Montout, Contribution au developpement d’une Approche Prédictive Locale de la crise d’ébullition, Doctorat de l’Université de Toulouse, 2009

[13] Maity, S. Effect of velocity and gravity on bubble dynamics. Master’s thesis, University
of California, Los Angeles, 2000

[14] Basu, N.,Warrier, G. R., and Dhir, V. K. Wall heat flux partitioning during subcooled flow boiling :
Part 1 - model development. Journal of Heat Transfer 127 (2005), 131–140.
Basu, N.,Warrier, G. R., and Dhir, V. K. Wall heat flux partitioning during subcooled flow boiling
Part 2 - model validation. Journal of Heat Transfer 127 (2005), 141–148

[15] Rohsenow, W. M. Heat transfer with evaporation. University of Michigan Press, 1953

[16] Legendre, D., Colin, C., and Coquard, T. Lift, drag and added mass of a hemispherical bubble sliding and growing on a wall in a viscous linear shear flow. Philosophical Transactions of the Royal Society A doi :10.1098/rsta.2008.0009 (2008).

Legendre, D., and Magnaudet, J. The lift force on a spherical bubble in a viscous linear shear flow.Journal of Fluid Mechanics 368 (1998), 81–126.

Legendre, D., Magnaudet, J., and Mougin, G. Hydrodynamic interactions between two spherical rising side by side in a viscous liquid. Journal of Fluid Mechanics 497 (2003), 133–166.

[17] Zuber, N. Hydrodynamic aspects of boiling heat transfer. PhD thesis, University of California, Los Angeles, 1959.

Zuber, N. The dynamics of vapor bubbles in nonuniform temperature fields. International Journal of Heat and Mass Transfer 2 (1961), 83–98.

[18] Situ, R., Mi, Y., Ishii, M., and Mori, M. Photographic study of bubble behaviors inforced convection subcooled boiling. International Journal of Heat and Mass Transfer 47 (2004), 3659–3667

[19] Unal, H. C. Bubble-departure diameter, bubble-growth time and bubble-growth rate during the subcooled nucleate flow boiling of water up to 177 bar. Tech. rep., Central Technical Institute TNO, P.O. Box 342, Apeldoorn, The Netherlands, 1973. Ref. No. 73-02829.

Unal, H. C. Maximum bubble diameter, maximum bubble-growth rate during the subcooled nucleate flow boiling of water up to 17.7 mn/m2. International Journal of Heat and Mass Transfer 19
(1976), 643–649.

[20] Boree, J., Charnay, G., Fabre, J., Legendre, D., and Magnaudet, J. Ecoulements diphasiques eau-vapeur avec changement de phase. Tech. rep., Rapport intermediaire IMFTInterface, 1992.