1992
DOI: 10.1016/0301-9322(92)90071-n
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Dynamic fluid flow behaviour of a tank draining through a vertical tube

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Cited by 15 publications
(10 citation statements)
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“…It should be noted that the model developed in this work is only applicable for the fully developed oscillatory¯ow, and thus that it cannot describe the behaviour for very small void fractions or for the large diameter downcomer. In these cases thē ow dynamics is diVerent and is determined by the behaviour of large gas bubbles at the top of the downcomer, as also observed previously [4].…”
Section: Fully Developed Oscillatory¯owmentioning
confidence: 64%
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“…It should be noted that the model developed in this work is only applicable for the fully developed oscillatory¯ow, and thus that it cannot describe the behaviour for very small void fractions or for the large diameter downcomer. In these cases thē ow dynamics is diVerent and is determined by the behaviour of large gas bubbles at the top of the downcomer, as also observed previously [4].…”
Section: Fully Developed Oscillatory¯owmentioning
confidence: 64%
“…The stages of the fully developed oscillatory process can be described intuitively, but they are con®rmed by the experimental observations in this work and the reported observations of the previous investigators [1,4]. The highly simpli®ed stages are shown diagrammatically in Fig.…”
Section: Qualitative Description Of the Processmentioning
confidence: 81%
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“…Another aspect worthy of investigation would consist in examining the influence of the neck's length. As shown by Tehrani et al (1992) , increasing this length may change the dynamics of oscillations by adding a large pressure loss in the system. How these changes are reflected in the dynamics of bubbles released from the neck is unknown and could be investigated with the methods employed here.…”
Section: Summary and Concluding Remarksmentioning
confidence: 99%
“…These studies focused on small d * , a condition under which the flow exhibits an on-off oscillatory behavior. Tehrani et al (1992) proposed a model aimed at predicting the pressure fluctuation amplitude in the top air buffer in an idealized configuration. In their work, the bottle is reduced to a cubic tank, with a typical size of 25 cm, and the neck to a 60 cm long straw with a diameter up to 25 mm, i.e.…”
Section: Introductionmentioning
confidence: 99%