Measurements of liquid hold-up and pressure drop are reported for stratified flow in a slightly inclined (0.65° and 2.1°), 5 cm pipeline. Velocity profiles in the gas phase have been determined for a limited number of flow conditions. Semi-empirical correlations are proposed for the transition to slug flow, the interfacial friction factor and the liquid hold-up. © 1987.
CITATION STYLE
Andreussi, P., & Persen, L. N. (1987). Stratified gas-liquid flow in downwardly inclined pipes. International Journal of Multiphase Flow, 13(4), 565–575. https://doi.org/10.1016/0301-9322(87)90022-X
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