Slug Initiation Evaluation in Long Horizontal Channels Experimentally
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Slug Initiation Evaluation in Long Horizontal Channels Experimentally

Authors: P. Adibi, M. R. Ansari, S. Jafari, B. Habibpour, E. Salimi

Abstract:

In this paper, the effect of gas and liquid superficial inlet velocities and for the first time the effect of liquid holdup on slug initiation position are studied experimentally. Empirical correlations are also presented based on the obtained results. The tests are conducted for three liquid holdups in a long horizontal channel with dimensions of 5cm10cm and 36m length. Usl and Usg rated as to 0.11m/s to 0.56m/s and 1.88m/s to 13m/s, respectively. The obtained results show that as αl=0.25, slug initiation position is increasing monotonically with Usl and Usg. During αl=0.50, slug initiation position is almost constant. For αl=0.75, slug initiation position is decreasing monotonically with Usl and Usg. In the case of equal void fraction of phases, generated slugs are weakly (low pressure). However, for the unequal void fraction of phases strong slugs (high pressure) are formed.

Keywords: Liquid holdup, Long horizontal channel, Slug initiation position, Superficial inlet velocity.

Digital Object Identifier (DOI): doi.org/10.5281/zenodo.1336520

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References:


[1] Y. Taitel, C. Sarica, J.P. Brill, "Slug flow modelling for downward inclined pipe flow: theoretical considerations", Int. J. Multiphase Flow 26, 2000, pp 833–844.
[2] D. Barnea, Y. Taitel, "A model for slug length distribution in gas-liquid slug flow", Int. J. Multiphase Flow 19, 1993, pp 829-838.
[3] O. J. Nydal, S. Pintus and P. Andreussi, "Statistical characterization of slug flow in horizontal pipes", Int. J. Multiphase Flow 18, No. 3, 1992, pp. 439-453,
[4] C.J. Crowley, G.B. Wallis, J.J. Barry, "Validation of a one-dimensional wave model for the stratified-to-slug flow regime transition, with consequences for wave growth and slug frequency", Int. J. Multiphase Flow 18, 1992, pp 249–271.
[5] A. Sanchis, G. W. Johnson, A. Jensen, " The formation of hydrodynamic slugs by the interaction of waves in gas–liquid two-phase pipe flow", Int. J. Multiphase Flow 37, 2011, pp 358–368.
[6] X. Wang, G. Liejin, X. Zhang, "An experimental study of the statistical parameters of gas–liquid two-phase slug flow in horizontal pipeline", (Technical Note), Int. J. Heat and Mass Transfer 50, 2007, pp 2439–2443.
[7] Z. Fan, F. Lusseyran, T.J. Hanratty, "Initiation of slugs in horizontal gas–liquid flows", AIChE J., 39 (11), 1993, pp 1741-1753.
[8] S.R. Davies, "Studies of Two-phase Intermittent Flow in Pipelines", Ph.D. Thesis, University of London., 1992.
[9] C.P. Hale, "Slug Formation, Growth and Collapse", Ph.D. Thesis, University of London., 2000.
[10] P. M. Ujang, Ch. J. Lawrence, C. P. Hale, G. F. Hewitt, "Slug initiation and evolution in two-phase horizontal flow", Int. J. Multiphase Flow 32, 2006, pp 527–552.
[11] M.R. Ansari, "Dynamical behavior of slug initiation generated by short waves in two-phase air–water stratified flow", ASME HTD 361, 1998, pp 289–295.
[12] M.R. Ansari, B. Arzandi, "Two-phase gas–liquid flow regimes for smooth and ribbed rectangular ducts", Int. J. Multiphase Flow 38, 2012, pp 118-125.