Download Advances in Multiphase Flow and Heat Transfer, Volume 2 by Lixin Cheng and Dieter Mewes (Ed) PDF

By Lixin Cheng and Dieter Mewes (Ed)

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2 (2009) Angeli Empirical correlations Quinn & Sigloh [26] found the organic phase holdup at inversion, ϕ IO , obtained in oil-in-water dispersions, decreases with the increase in agitation speed before reaching a constant value at high agitation speeds, according to: ϕ IO = ϕ 0 + c P (1) where φ0 is the asymptotic phase inversion holdup at high agitation speed, P is the 3 power input ( ∝ ρ m N I where ρm is mixture density and NI is the agitation speed) and c is a constant determined by the physical properties of the system which could be approximately related to the Weber number.

2”, Nuclear Technology, vol. 127, pp. 160 -169, 1999. S. Oh and S. T. Revankar, “Effect of noncondensable gas in a vertical tube condenser”, Nuclear Eng. Design, vol. 235 pp. 1699 – 1712, 2005. Oh and S. T. Revankar, “Experimental and theoretical investigation of film condensation with noncondensable gas”, Intern. J. Heat Mass Transfer, vol. 49, pp. 2523-2534, 2006. W. Nusselt, “Die oberflachenkoondensation des wasserdampfes”, Z. Ver. , vol. Vol. 60, pp. 541-546, 1916. W. M. Rohsenow, “Heat transfer and temperature distribution in laminar film condensation”, Trans ASME, vol.

Ortega, M. Muselli, I. Milimouk and D. Beysens, “Study of dew water collection in humid tropical Islands”, Journal of Hydrology vol. 361, pp. 159– 171, 2008. K. D. Giovannelli, Heat pipe heat exchanger design theory heat transfer equipment design, Washington DC: Hemisphere pp. 609–653, 1988. L. L. Vasiliev, “Heat pipes in modern heat exchangers”, Applied Thermal Engineering, vol. 1–19, 2005. F. V. Kosoy, “Refrigerating heat pipes”, Applied Thermal Engineering vol. 21 pp. 631-641, 2001. General Electric Company, “Refrigeration passive defrost system”, US Pat.

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