Bounds on Two-Phase Flow: Part I — Frictional Pressure Gradient in Circular Pipes

Author:

Awad M. M.1,Muzychka Y. S.1

Affiliation:

1. Memorial University of Newfoundland

Abstract

Simple rules are developed for obtaining rational bounds for two-phase frictional pressure gradient. Both the lower and upper bounds are based on the separate cylinders formulation. The lower bound is based on turbulent-turbulent flow that uses the Blasius equation to represent the Fanning friction factor. The upper bound is based on an equation that represents well the Lockhart-Martinelli correlation for turbulent-turbulent flow. The model is verified using published experimental data of two-phase frictional pressure gradient versus mass flux at constant mass quality. The published data include different working fluids such as R-12 and R-22 at different mass qualities, different pipe diameters, and different saturation temperatures. It is shown that the published data can be well bounded for a wide range of mass fluxes, mass qualities, pipe diameters and saturation temperatures. The bounds models are also presented in a dimensionless form as two-phase frictional multiplier (φl and φg) versus Lockhart-Martinelli parameter (X) for different working fluids such as R-12, R-22, air-oil and air-water mixtures.

Publisher

ASMEDC

Reference28 articles.

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2. Lockhart R. W. , and MartinelliR. C., 1949, “Proposed Correlation of Data for Isothermal Two-Phase, Two-Component Flow in Pipes,” Chemical Engineering Progress Symposium Series, 45 (1), pp. 39–48.

3. Martinelli R. C. , and NelsonD. B., 1948, “Prediction of Pressure Drop during Forced-Circulation Boiling of Water,” Trans. ASME, 70 (6), pp. 695–702.

4. Tong, L. S., 1967, Boiling Heat Transfer and Two-Phase Flow, John Wiley & Sons, Inc., New York.

5. Wallis, G. B., 1969, One-Dimensional Two-Phase Flow, McGraw-Hill Book Company, New York.

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