Abstract
Experiments of gas-liquid flow in a circular pipe for horizontal and inclined positions (upward/downward) are reported. The characteristics of two-phase flow in terms of liquid holdup (epsilon((L))) and induced flow patterns are studied using three experimental techniques; time-averaged epsilon((L)) from permittivity profiles using electrical capacitance tomography (ECT), instantaneous epsilon((L)) using two fast-closing valves (TFCV), and high-speed camera images (HSCI) to capture/identify the formed flow patterns. Thus, this experimental setup enables the development of more well-defined flow patterns in gas-liquid two-phase flow and allows for multi-technique verification of the results. Taken from experimental measurements, a model is proposed to predict epsilon((L)) for high and low situations. The correlations are a function of the hydrodynamic dimensionless quantities which provide hydrodynamic similarity. Regarding different pipe orientations, epsilon((L)) predictions are comparable to epsilon((L)) from experimental measurements with accepted accuracy: 88% of the predictions are within +/- 5-15% and 98% are below +/- 20%. The correlations also were validated by reported results and against correlations available in the literature and show higher prediction accuracy. It is confirmed that the kinematic similarity which is achieved by the gas-liquid velocity ratios and the inertial forces influence the flow pattern and the liquid holdup.