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Showing papers on "Slug flow published in 1968"


Journal ArticleDOI
TL;DR: In this paper, the axial dispersion coefficient was measured in water filled bubble columns of 5·08, 14·0 and 29·0 cm dia. as a function of the superficial gas velocity.

101 citations



Journal ArticleDOI

4 citations


Journal ArticleDOI
TL;DR: In this article, an electrical void-meter based on transducement of void fraction into impedance is employed to measure the void distribution along a heater in an annular channel.
Abstract: Farther basic knowledge has been gained on the behavior of two-phase flow through the follow-ing experiments. An electrical void-meter based on transducement of void fraction into impedance is employed to measure the void distribution along a heater in an annular channel.Experiments have further been conducted on the "velocity slip ratio (V0/V1)" to correlate the void-fraction (Rg) with the volume flow rate ratio (Fg). The resulting equation takes the form Rg= 0.92•Fg, and the ratio V0/V1 = 1.08, for slug flow in a vertical pipe.Statistical methods have been applied in analyzing the two-phase flow. It is shown that the speed of voids in a two-phase flow can be determined with a cross-correlation function calculated from two time series of void-fraction fluctuation measured at two points along the channel.

3 citations


Journal ArticleDOI
TL;DR: In this paper, the authors measured the steam volume fraction α of a two phase mixture flowing upward under atmospheric pressure in a vertical concentric annulus, with inner and outer diameters respectively 9.5mm and 21mm.
Abstract: The steam volume fraction α of a two phase mixture flowing upward under atmospheric pressure was measured in a vertical concentric annulus, with inner and outer diameters respectively 9.5mm and 21mm. Use was made of a capacitance type void meter described in a previous paper, and the following correlation was obtained:α=1-√(1-x)3/1+Kx, where K=eρl/ρgV0.50exp (-2×10-6q)e=1.3 (bubble flow), e=1 (slug flow and annular flow)x is the steam weight fraction, ρl/ρg the density ratio of liquid to steam, V0 the superficial velocity (m/s), and q the heat flux (kcal/mm2·hr).The experimental data obtained under high pressure by several investigators for various channel forms correlated very well with use of the formulaK=eρl/ρgV0.50, where e is the same as mentioned above.These correlations are very useful for predicting the steam volume fraction at various pressures below 2, 000 psia.

2 citations


Journal ArticleDOI
TL;DR: In this article, the normalized temperature distribution for slug flow in all regular polygonal channels with uniform heat flux at the walls is shown to be the same as that for all triangular channels.

1 citations