By Lixin Cheng and Dieter Mewes (Ed)
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Additional resources for Advances in Multiphase Flow and Heat Transfer, Volume 2
Vol. 24, pp. 1959–1968, 2004. Y. C. Ng and H. Bao, “Thermal performance of a flat-plate heat pipe collector array”, J. Solar Energy vol. 50, pp. 491–498, 1993. T. A. Ozbolt, US Lab Architecture Control Document, Volume 7: Temperature and Humidity Control, Revision New, D683-14719-1-7, Huntsville, Alabama: Boeing Defense and Space Group, Missile & Space Division, December 20, 1996. Passive Condensers Advances in Multiphase Flow and Heat Transfer Vol. 2 (2009) 35                  M.
Liu, N. E. Todreas and M. J. Driscoll, An experimental investigation of a passive cooling unit for nuclear plant containment, Nuclear Eng. Design, vol. 199, pp. 243-255, 2000. K. Vierow and V. E. Schrock, “condensation in a natural circulation loop with noncondensable gas present: Part I - Heat transfer”, Japan - U. S. ) 1992. S. 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.
Models based on drop breakage and coalescence rates It has been found that factors which affect drop coalescence and break up , such as agitation speed, wettability, impeller type, liquid properties and electrostatic interactions, also affect the phase inversion point and the width of the ambivalent range ( ). This has led investigators to consider phase inversion as an imbalance between break up and coalescence of the dispersed drops [5, 27]. In a dilute O/W dispersion, for example, a dynamic balance will exist between drop break up and coalescence.