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By Lixin Cheng; Dieter Mewes

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Z. E. F. Peterson, “An investigation of condensation from steam–gas mixtures flowing downward inside a vertical tube”, Nuclear Eng. Design, vol. 177, pp. 53–69, 1997. H. Araki, Y. Kataoka and M. Murase, "Measurement of condensation heat transfer coefficient inside a vertical tube in the presence of noncondensable gas", J. Nuclear Science and Technology, Vol. 32, pp. 78-91, 1995. H. A. S. Kazimi and M. W. Golay, "Forced Convection In-Tube Steam Condensation in Presence of Noncondensable Gases”, Int.

Secondary dispersions increase the effective dispersed phase hold up, since part of the continuous phase is trapped within the dispersed, and can cause inversion at lower dispersed phase fractions than when they are not present. Kumar [14] attributed the formation of secondary dispersions to the differences of dielectric constants of the two immiscible phases. Oil drops experience repulsive forces due to the overlapping of the electrical double layers that form around the drops in the water phase and have low coalescence efficiency.

Revankar, S. Oh, W. Zhou and G. Henderson, “Condensation correlation for a vertical passive condenser system”, in Proc. 2008 International Congress on Advances in Nuclear Power Plants (ICAPP '08), American Nuclear Society, ANS Annual Meeting, Anaheim, California, USA, June 8-12, 2008. Advances in Multiphase Flow and Heat Transfer Vol. 2 (2009) 38-61 38 Chapter 2 Phase Inversion in Liquid-Liquid Pipe Flows Panagiota Angeli∗ Department of Chemical Engineering, University College London Torrington Place, London WC1E 7JE, UK.

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