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Journal ArticleDOI

Effect of tube diameter on flooding

01 May 2001-International Journal of Multiphase Flow (Pergamon)-Vol. 27, Iss: 5, pp 797-816
TL;DR: In this article, the effect of tube diameter on the mechanism of flooding in vertical gas-liquid countercurrent annular flow was investigated. But the results indicated that the mechanism was qualitatively different in the small and the large diameter test sections.
About: This article is published in International Journal of Multiphase Flow.The article was published on 2001-05-01. It has received 56 citations till now.
Citations
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Journal ArticleDOI
TL;DR: In this article, a falling water film is sheared by a turbulent counter-current air flow in an inclined rectangular channel and the influence of the air flow on controlled traveling waves consisting of a large wave hump preceded by capillary ripples is investigated.

24 citations

Journal ArticleDOI
TL;DR: In this paper, a model for interfacial wave propagation for a liquid film on the wall of a vertical pipe and for a flowing gas in the central core was derived for a flat interface, and for traveling waves on the interface.

16 citations

Journal ArticleDOI
TL;DR: In this article, the complex liquid film behaviors at flooding in an inclined pipe were investigated with computational fluid dynamic (CFD) approaches, including the dynamic wave characteristics before flooding and the transition of flow pattern when flooding happened.

15 citations

Journal ArticleDOI
TL;DR: In this article, measurements of the pressure gradient, film thickness and down flow rate were made for a range of air and water flow rates under pre- and post-flooding conditions.

14 citations

References
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Journal ArticleDOI
TL;DR: In this paper, an assessment of the various viewpoints on the slug-to-churn flow transition in vertical upward flow in the light of recent experimental results obtained at Harwell Laboratory is made.

173 citations

Journal ArticleDOI
H.J. Richter1
TL;DR: In this article, a new flooding correlation is presented which solves the obvious contradiction between the Wallis correlation and the study by Pushkina and Sorokin concerning the scaling question at zero penetration of liquid.

146 citations


"Effect of tube diameter on flooding..." refers methods in this paper

  • ...Richter (1981) and Jayanti et al. (1996) suggested, based on di€erent arguments, that the Wallis-type correlation would work well in small diameter tubes and the Kutateladze-type in large diameter tubes....

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Book ChapterDOI
TL;DR: In the absence of electromagnetic force fields, thermocapillary effects or concentration-capillary effects, countercurrent flow can be sustained only as a result of the difference in the gravitational force per unit volume on the gas and on the liquid as discussed by the authors.
Abstract: Countercurrent flow of a gas and a liquid in direct contact with each other is, of necessity, gravity dominated. That is, in the absence of electromagnetic force fields, thermocapillary effects, or concentration-capillary effects, countercurrent flow can be sustained only as a result of the difference in the gravitational force per unit volume on the gas and on the liquid. If the gas and liquid are simultaneously introduced into a porous medium or into a vertical or inclined pipe, the gas tends to rise relative to the liquid. If conditions allow complete separation, it is possible to maintain steady countercurrent flow in which the liquid discharges at the bottom while the gas flows out from the top. The countercurrent flow is opposed by interfacial friction between the phases, which always seems to increase monotonically as the relative countercurrent mean velocity of the phases increases. Hence, for a given geometry and liquid-gas pair, there is a maximum relative velocity that can be sustained in countercurrent flow. This point is known as the onset of flooding. Further increases in gas or liquid input ratas result in only partial delivery of the liquid out of the bottom. Eventually, if the gas velocity becomes sufficiently high, none of the liquid is delivered at the bottom, and fully cocurrent upward flow is established. If the liquid is being introduced from an upper plenum, none will penetrate into the pipe or porous medium when this second critical gas velocity is reached.

117 citations

Journal ArticleDOI
TL;DR: In this paper, the authors investigated the effect of tube end geometries on measured countercurrent fluxes, liquid fraction, and pressure gradients, and analogies between countercurrent gas-liquid flow and other more familiar flows in internal geometry are indicated.

108 citations

Journal ArticleDOI
TL;DR: In this paper, a 32 mm dia vertical pipe with various forms of liquid outlet, namely a porous wall, a tapered outlet, and a square-edged outlet, was used to investigate the effect of churn flow on the penetration rate.

103 citations


"Effect of tube diameter on flooding..." refers background or methods in this paper

  • ...For example, McQuillan et al. (1985) and Govan et al. (1991) , among others, used slight depressurization , of the order of 0.05 bar, to induce ¯ooding while others such as Dukler and Smith (1982) and Zabaras and Dukler (1988) induced ¯ooding by gradually increasing the air ¯ow rate....

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  • ...It is generally believed (Suzuki and Ueda, 1977; McQuillan et al., 1985; Govan et al., 1991) that ¯ooding occurs when large waves, formed near the liquid outlet, are swept upwards by the gas phase....

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  • ...In some cases, this discrepancy can be attributed to the inlet and outlet conditions for the gas and liquid phases (Govan et al., 1991), however, the experiments of International Journal of Multiphase Flow 27 (2001) 797±816 www.elsevier.com/locate/ijmul¯ow Biage (1989) showed that even with smooth…...

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  • ...The ®rst mechanism, namely, upward transport of ring-type waves, has been observed, among others, by Suzuki and Ueda (1977), McQuillan et al. (1985) and Govan et al. (1991)....

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  • ...As a modi®cation to (ii) above, Govan et al. (1991) de®ned ¯ooding as the point at which liquid appeared (and not necessarily carried away by the gas stream) above the liquid injection point....

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