An Experimental and Theoretical £ Investigation of Annular Steam ...
An Experimental and Theoretical £ Investigation of Annular Steam ...
An Experimental and Theoretical £ Investigation of Annular Steam ...
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The experimental part <strong>of</strong> this report (chapter 3) is an<br />
attempt to rectify this lack <strong>of</strong> a consistent set <strong>of</strong> film flow<br />
data achieved with steam-water at high pressures. More than 200<br />
film flow measurements are presented, <strong>and</strong> they are accompanied<br />
by experimental values <strong>of</strong> pressure gradients, film thicknesses,<br />
wave frequencies <strong>and</strong> velocities, <strong>and</strong> burnout heat fluxes. The<br />
experiments were carried out under both adiabatic <strong>and</strong> diabatic<br />
conditions in one annular <strong>and</strong> two tubular geometries.<br />
On the basis <strong>of</strong> these data, a film-flow model for the prediction<br />
<strong>of</strong> burnout in tubes <strong>and</strong> annuli is developed in the analytical<br />
part <strong>of</strong> the report (chapter 4). Finally, the capability<br />
<strong>of</strong> the model is shown by comparisons <strong>of</strong> predicted <strong>and</strong> experimental<br />
values.<br />
2. ANNULAR TWO-PHASE FLOW<br />
The flow regime, which is characterized by the presence <strong>of</strong><br />
a liquid film adjacent to the channel wall, is called the annular<br />
two-phase flow regime. This chapter only deals with the<br />
general aspects <strong>of</strong> annular flow in a very superficial way. A<br />
detailed description <strong>of</strong> this topic (especially regarding airwater<br />
systems) is given by Hewitt <strong>and</strong> Hall-Taylor (1970). The<br />
terminology used in the present report follows to a great<br />
extent that used in chis recommendable textbook.<br />
2.1. Flow Regimes<br />
The evolution <strong>of</strong> the annular flow pattern is illustrated in<br />
conceptual form in fig. 2.1. Here a tube is shown with a heated<br />
wall, where the liquid is introduced at the bottom.<br />
The first generation <strong>of</strong> steam takes place by nucleation at<br />
the wall, producing steam bubbles. As the fluid proceeds up the<br />
tube, further generation <strong>of</strong> steam takes place, <strong>and</strong> the small<br />
bubbles coalesce into bullet-shaped bubbles called slugs. After<br />
the slug flow regime, a transition region called the churn flow<br />
regime is reached. This flow pattern is a result <strong>of</strong> instabilities<br />
in the slugs due to the increase <strong>of</strong> the steam velocity.<br />
It is characterized by a "churning" or oscillatory action.<br />
After this transition region, the annular flow regime is<br />
established. It is seen that the liquid film is strongly agi-