[1] Incropera, Frank P., Adrienne S. Lavine, and David P. DeWitt. Fundamentals of heat and mass transfer. John Wiley & Sons Incorporated, 2011.

[2] Kutateladze, S. S., Kotloturbostroenie, 3, 10, 1948.

[3] Zuber, N., Trans. ASME, 80, 711, 1958

[4]  Zhuravlev A.S. Heat transfer in pool boiling of propane under the conditions of different saturation pressures, Journal of Engineering Physics and Thermophysics. Vol. 73. No. 2, 2000

[5]  Frost W. and Dzakowic G. S., "An Extension of the Method of Predicting Incipient Boiling on Commercially Finished Surfaces," in ASME/AIChE Heat Transfer Conference, Paper 67-HT-61, 1967.

[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] 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

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

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

[10] Morgan, V. T., The Overall Convective Heat Transfer from Smooth Circular Cylinders, in T. F. Irvine and J. P. Hartnett, Eds., Advances in Heat Transfer, Vol. 11, Academic Press, New York, 1975, pp. 199–264.

[11] Churchill, S. W., and H. H. S. Chu, Int. J. Heat Mass Transfer, 18, 1049, 1975.

[12] Pérez Mañes J. et al, Validation of NEPTUNE-CFD Two-Phase Flow Models Using Experimental Data, Hindawi Publishing Corporation, Science and Technology of Nuclear Installations, Volume 2014, Article ID 185950, 19 pages.

[13] Global Digital Central Encyclopedia, Thermal fluid central, available at