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KURENAI : Kyoto University Research Information Repository

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M. 1 INTRODUCTION<br />

A loss of coolant accident (LOCA) and subsequent rewetting and ref-<br />

looding phenomena in a nuclear reactor constitute another important phases<br />

of the nuclear reactor accident. In this case, large amount of vapor<br />

is generated and high quality two-phase flow often encountered.<br />

Powerlevels under these accidents are relatively low (decay heat level)<br />

and the transient process is slow. Under these circumstances, the boil-<br />

ing and two-phase flow phenomena are not localized , but depend on the<br />

upstream conditions. In the nuclear reactor core, the heated length is<br />

considerably long extending to several meters. Therefore, the boiling and two-phase<br />

flow phenomena involved are those for large length to diameter ratio, 2/dhe'<br />

The heat and mass transfer mechanisms are considered to be quite different<br />

from those for small 2/dhe which have been studied in the previous chapters.<br />

The transient and steady state boiling phenomena under these large<br />

2/dhe conditions are basically determined by the mass, momentum and energy<br />

transfer processes of annular or annular dispersed flowswhich are usually<br />

observed in high quality two-phase flow.<br />

Therefore, in this chapter and succeeding two chapters (Chapter 1V<br />

and V), the hydrodynamic characteristics' of annular or annular dispersed<br />

flow are studied. Several practical correlations which are ne-<br />

cessary to the analyses of nuclear reactor accidents have been developed.<br />

Firstly, the droplet size and its distribution are analysed in this chapter.<br />

An accurate knowledge of the mean droplet size and droplet size distri-<br />

bution is essential to the detailed analyses of droplet or annular dispersed<br />

flow. The inception of droplet entrainment from the liquid film significantly<br />

changes the mechanisms of mass, momentum and energy transfer [1,2]. The avail-<br />

able Interfacial area and droplet transport depend on the amount of entrain-<br />

ment and droplet size. Therefore, in order to accurately model and predict a<br />

number-of important physical phenomena in annular dispersed flow, an under-<br />

standing of mechanisms of entrainment, generation of droplets and size dis-<br />

tribution are prerequisite. In particular, the relative velocity and droplet<br />

carryover, the dryout and post dryout heat transfer [3-7] and the effective-<br />

ness of the emergency core cooling in light water reactors [8-11] are signif-<br />

155

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