logo

Two-phase slug flow in vertical and inclined tubes

Two-phase slug flow in vertical and inclined tubes

Xia Guo-Dong
Zhou Fang-De
Hu Ming-Sheng
Nuclear Science and TechniquesVol.7, No.4pp.232-237Published in print 01 Nov 1996
42103

Gas-liquid slug flow is investigated experimentally in vertical and inclined tubes. The non-invasive measurements of the gas-liquid slug flow are taken by using the EKTAPRO 1000 High Speed Motion Analyzer. The information on the velocity of the Taylor bubble, the size distribution of the dispersed bubbles in the liquid slugs and some characteristics of the liquid film around the Taylor bubble are obtained. The experimental results are in good agreement with the available data.

Gas-liquid two-phase flowVertical tubesInclined tubesTaylor bubble
References
1 Fernandes R C.

Experimental and theoretical studies of isothermal upward gas-liquid slug flows in vertical tubes

. Ph D Dissertation, University of Houston, Texas, 1981
Baidu ScholarGoogle Scholar
2 Dukler A E, Moalem Maron D, Brauner N. Chem Engng Sci, 1985; 40: 1379
3 Mao Z S, Dukler A E. Experiments in Fluids, 1989; 8: 169
4 Taitel Y, Barnea D.

Two phase slug flow

. In: Hartnett J P, Irvine T F, eds. Advance in heat transfer, Vol.20. New York: Academic Press, 1990; 83
Baidu ScholarGoogle Scholar
5 Bendiksen K H. Int J Multiphase Flow, 1984; 10: 467
6 Bonnccazc R H, Erskinc W, Greskovich E J. Am Inst Chem Engng J, 1971; 17: 1109
7 Zukoski E E. J Fluid Mech, 1966; 25: 821
8 Nicklin D J, Wilker J O, Davidson J F. Trans Inst Chem Engrs, 1962; 40: 61
9 Davies R M, Taylor G I. Proceedings of the Royal Society, London, 1950; Vol.200, series A, p375
10 Ozgu M R, Chen J C, Stenning A H. J Heat Transfer, Trans ASME, Series C, 1973; 8: 425