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Extra resources for Advances in multiphase flow and heat transfer Vol. 1, 2009

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A. Hughmark, "Holdup in gas-liquid flow," Chemical Engineering Progress, vol. 58, pp. 62-65, 1962. A. Premoli, D. Francesco, and A. Prima, "An empirical correlation for evaluating two-phase mixture density under adiabatic conditions," in European Two-Phase Flow Group Meeting, Milan, Italy, 1970. A. I. Filimonov, M. M. Przhizhalovski, E. P. Dik, and J. N. Petrova, "The driving head in pipes with a free interface in the pressure range from 17 to 180 atm," Teploenergetika, vol. 4, pp. 22-26, 1957.

40, pp. 61-68, 1962. J. Schmidt, H. Giesbrecht, and C. W. M. van der Geld, "Phase and velocity distributions in vertically upward high-viscosity two-phase flow," International Journal of Multiphase Flow, vol. 34, pp. 363-374, 2008. Advances in Void Fraction, Flow Pattern Maps and… Advances in Multiphase Flow and Heat Transfer Vol. 1 (2009) 49 [28] [29] [30] [31] [32] [33] [34] [35] [36] [37] [38] [39] [40] [41] [42] R. D. thesis, University of Tulsa, Tulsa, Oklahoma, 1994. R. C. D. thesis, University of Houston, Houston, Texas, 1981.

27, Witte et al. [73] measured a value of 3169 W m-2 K-1 for the two-phase heat transfer coefficient (hTP). The following example calculation illustrates the use of the general two-phase heat transfer correlation, Eq. (24), to predict the hTP value measured by Witte et al. [73]. 40  10 4 m G  m L Equations (19) and (18) are then used for calculating the flow pattern factor (FP), 44 Advances in Multiphase Flow and Heat Transfer Vol. 730 and The inclination factor (I *) has a value of one in horizontal tube (θ = 0).

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