L - KTH
L - KTH
L - KTH
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42 C.J. WOOD<br />
With the suction piping filled, circulation and heatup proceed in the same manner as for<br />
the discharge side. For this phase, flow enters the system in the same location but<br />
travels up the suction piping of the first loop, into and around the annulus and back down<br />
the suction llne of the second loop. Unlike the discharge side, all parts of this<br />
circulating loop are exposed to full system flow. Chemical injection, process monitoring,<br />
and subsequent cleanup are all controlled in the same manner as the discharge side. Flow<br />
reversals, although not as important, are still performed at regular intervals.<br />
If the annulus cannot be included in the flow path, the approach for performing the<br />
suction decontamination is almost identical to that described for the discharge side<br />
without a cross-tle llne. A "sloshing" technique is used to move fluid from one loop to<br />
the other and hold it at the maximum elevation for a short period of time. One additional<br />
problem with the suction side is the accuracy of the level control. If the fluid cannot<br />
enter the annulus it is important that the equipment be able to control the maximum fluid<br />
levels very accurately. Otherwise, much of the benefit of the application can be lost<br />
(from levels which are too low) or problems "can be encountered with fluid ~n the annulus<br />
(from levels which are too high).<br />
3.1.2 Single Phase RWR Decontaminations For decontaminations that are coincident with<br />
major modifications or complete piping replacements, a single phase application may be more<br />
appropriate. In order to accomplish this, however, additional connection points must be<br />
made available. A number of potential connection points is possible depending upon the<br />
specific needs and concerns of the individual utility. Usually twelve additional<br />
connections are necessary. One is located on each of the ten discharge risers as close to<br />
the penetration into the vessel as possible. The remaining two are located at the suction<br />
nozzles. With these additional connections both the suction and discharge sides can be<br />
decontaminated simultaneously and fresh reagent supplied to virtually all portions of the<br />
system. A typical flowpath is shown in Fig. 3.<br />
The major advantages of this approach are the potential for critical path savings since<br />
only one heatup, injection, circulation, and cleanup step is required and the improved DFs<br />
achieved in the risers from direct injection of fresh reagents. This must, however, be<br />
balanced against the additional effort, time, expense and radiation exposure required to<br />
prepare for this approach.<br />
3.2 PWR steam generator channel head applications<br />
Decontaminations are performed in the channel heads of PWRs to reduce the amount of<br />
radiation exposure necessary to complete major maintenance activities at the tubesheet on<br />
the primary side (e.g. sleeving, plugging etc.). To maximize the benefit, two to three<br />
feet of the tubes above the bottom of the tubesheet need to be exposed to the reagent.<br />
Fig. 3. BWR reactor water recirculatlon system two<br />
phase decontamination flowpath