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Regional Basic Professional Training Course in Korea

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❙ 519 ❙<br />

8-B. Determ<strong>in</strong>istic Accident Analysis (LOCA)<br />

The rate of depressurization decreases as the difference between vessels and conta<strong>in</strong>ment<br />

pressures decreases. The rate of steam generation due to flash<strong>in</strong>g decreases, the rate of<br />

liquid dump<strong>in</strong>g <strong>in</strong>to the lower plenum <strong>in</strong>creases, and the sweepout rate decreases. Very<br />

little ECC <strong>in</strong>jection is bypassed out the break; most of it flows to fill the downcomer and<br />

lower plenum.<br />

(3) Reflood phase<br />

The core beg<strong>in</strong>s to reflood with ECC water after the lower plenum is filled. Initially, core<br />

refill is quite rapid because the downcomer is ma<strong>in</strong>ta<strong>in</strong>ed full by the cont<strong>in</strong>ued ECC<br />

<strong>in</strong>jection and there is very little resistance <strong>in</strong> the <strong>in</strong>tact loop because there is no steam<br />

flow and no liquid to vaporize <strong>in</strong> the steam generator.<br />

Due to high temperatures of fuel rods, the thermal regimes <strong>in</strong> the core dur<strong>in</strong>g reflood<br />

encompass the entire spectrum start<strong>in</strong>g with s<strong>in</strong>gle liquid and progress<strong>in</strong>g with nucleate<br />

boil<strong>in</strong>g, transition boil<strong>in</strong>g, film boil<strong>in</strong>g, churn twe‐phase flow, dispersed droplet flow and<br />

s<strong>in</strong>gle phase steam flow as shown <strong>in</strong> Figure 8.7‐4. Due to droplet deentra<strong>in</strong>ment at the tie<br />

plate and grid spacers, top‐quench<strong>in</strong>g and local quench<strong>in</strong>g occur <strong>in</strong> addition to the bottom<br />

one. Higher vapor velocities and liquid entra<strong>in</strong>ment occur <strong>in</strong> the central region of the core<br />

due to higher powered fuel rods. The entra<strong>in</strong>ed liquid has a beneficial cool<strong>in</strong>g effect.<br />

Some of the entra<strong>in</strong>ed liquid is deentra<strong>in</strong>ed at the upper tie plate. The rema<strong>in</strong>der is carried<br />

<strong>in</strong>to the upper plenum, where it is deentra<strong>in</strong>ed, form<strong>in</strong>g a two‐phase pool. Liquid from the<br />

pool can reenter the low power regions of the core because of the lower vapor velocities.<br />

As a result, a 3‐D flow pattern is established. Liquid from the two‐phase pool <strong>in</strong> upper<br />

plenum may be entra<strong>in</strong>ed by vapor and carried over to hot legs. In travers<strong>in</strong>g the upper<br />

plenum it can be deentra<strong>in</strong>ed on upper plenum structure.<br />

As the bottom quench progresses upward through he core, more liquid is carried over to

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