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KURENAI : Kyoto University Research Information Repository

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N. 1 INTRODUCTION<br />

As mentioned in the previous chapter, an accurate knowledge of the<br />

hydrodynamics of an annular and annular dispersed flow is the key f-actor<br />

in analysing the transient boiling and two-phase flow phenomena associated<br />

with a LOCA in a nuclear reactor. Mass, momentum and energy transfer pro-<br />

cesses in the annular and annular dispersed flow are strongly affected by<br />

the amount of droplet in the streaming gas flowing in the flow core [1,2].<br />

In particular, an accurate knowledge of entrainment is indispensable for<br />

the prediction of dryout and post dryout heat transfer [3-8] and for the<br />

evaluation of the effectiveness of emergency core cooling in light water<br />

reactors E9-12].<br />

Based on the mechanistic model of shearing off of roll-wave by the<br />

streaming gas, correlations are obtained for the inception of droplet ent-<br />

rainment [13], and for the amount of entrained droplet for a steady state<br />

flow condition [2]. The mean droplet size and its distribution [14] which<br />

are the important parameters in analysing the heat and mass transfer pro-<br />

cesses in boiling two-phase flow with high steam quality have been invest-<br />

igated in the previous chapter.<br />

On the other hand, the liquid film flow rate on a heated surface is<br />

another important parameter in evaluating the heat and mass transfer and<br />

the dryout heat flux in annular and annular dispersed flow. The amount<br />

of the liquid film flow r'ate is determined by the integral balance between _<br />

the droplet entrainment rate and the deposition rate. As for the deposition<br />

rate of droplet in a streaming gas, there have been many experimental and<br />

theoretical works and satisfactory correlations have been developed [1,15-28].<br />

However, the process of the entrainment seems more complicated and thus the<br />

efforts to develop a reliable entrainment rate correlation have not been very<br />

successful. The lack of such a correlation has been the main difficulty of<br />

a detailed,analysis of various phenomena in transient annular two-phase flow<br />

or in a post dryout regime. The main objective of this chapter isto develop<br />

a reliable correlation for entrainment rate from the liquid film. In the<br />

case of LWR transients and accidents, annular flow-or droplet flow may be en-<br />

countered under various conditions. Therefore, a general correlation cover-<br />

ing a wide range of flow conditions including entrance effects is highly de-<br />

sirable. As a first step, an entrainment rate correlation has been developed<br />

for relatively low viscous fluid such as water where the entrainment of drop-<br />

lets is generated mainly by the shearing-off of roll wave-crests.<br />

193

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