1971 Volume 14 Issue 71 Pages 447-454
Experimental and theoretical studies of the fluctuation of air-water two-phase slug flow in a vertical tube, have been described in three papers. Among them, the experimental results are presented in this paper. It was verified that the time variation of pressure drop is predicted by the variation of lengths of gas bubble and liquid slug flowing in the tube. It was also shown that the probability distribution of pressure drop in long segments of tube is normal distribution, and that in short segments, distribution has generally two peaks at Δp* (i.e., dimensionless pressure drop) =0 and 1. The maximum amplitude of the pressure drop was given by the following empirical equation δΔpmax*/Δpm*=0.7LT-0.62wl0-0.62wg00.9 where, δΔpmax* and Δpm* are the maximum amplitude and the mean value of dimensionless pressure drop, respectively; wl0 and wg0 superficial liquid and gas velocity, respectively; and LT is the length of segment of tube.
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