L - KTH
L - KTH
L - KTH
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68 C.J. Wo~,~<br />
Comparative costs (LOMI) decontamination for IX resins, transport and burial are as<br />
follows:<br />
BWR recirc system $ 80,000<br />
Full system - fuel out 1,300,000<br />
- fuel in 6,400.000<br />
PWR reclrc system $ 120,000<br />
Full system - fuel out 635,000<br />
- fuel in 1,300.000<br />
Waste management is one of the key issues associated with full system decontamination.<br />
Considerable progress is being made in improving waste disposal technology, including ion-<br />
specific resins, volume reduction and interim storage, any of which could significantly<br />
reduce costs. However, the high cost penalty associated with the fuel-in case is one of<br />
the main reasons why most utilities will initially opt for fuel removal.<br />
8.5 Materials compatibility<br />
As a result of extensive corrosion test programs by the BWR Owners Group for<br />
Intergranular Stress Corrosion Cracking research, the BWR position is considerably more<br />
advanced than the PWR situation. Recently-completed tests on highly irradiated stainless<br />
steels filled the last remaining gap in the BWR data base. These tests used 304 stainless<br />
steel which is susceptible to Irradlation-asslsted stress corrosion cracking (IASCC).<br />
Neither CAN-DECON nor LOMI had any adverse effects on these materials (30,37).<br />
A recent evaluation of the corrosion data has led General Electric to conclude that the<br />
risks associated with the use of the LOMI process for full system decontamination wlth the<br />
fuel removed are low provided that a plant-speclfic material review of all LOMl-wetted<br />
surfaces Is performed to verify the applicability of the existing data base (see Appendix<br />
A).<br />
Unfortunately the PWR data base is less complete. In particular corrosion data in the<br />
presence of boric acid is lacking, and there are no data at the high flow rates expected<br />
when the reactor coolant pumps are used to circulate the decontamination solvent. A two-<br />
year industry-funded program has been initiated with Westinghouse to evaluate corrosion<br />
issues.<br />
8.6 Cost benefit<br />
Cost-beneflt evaluations (56) for a number of decontamination scenarios are shown in<br />
Figures 8-4 to 8-7, including estimates for BWR decontaminations using the LOMI and CAN-<br />
DECON processes. The three options are (i) reclrculatlon piping system, (2) full system<br />
Including fuel, and (3) full system with fuel removed. For these calculations the<br />
reference plant was Quad Cities for an outage with above average maintenance requirements.<br />
Figures 8-8 to 8-11 show estimates for PWR decontamination, using Zion as a reference<br />
plant. The four options in this case are (1) steam generator channel heads, (2) full<br />
system including fuel, (3) full system wlth fuel removed, and (4) as (3) but for the<br />
special case of steam generator replacement.<br />
For each example, costs include vendor charges, waste disposal and critical path time at<br />
$624,000 per day. Savings include rents saved at $10,000/man-rem and critical path<br />
savings. The net benefit is savings less costs. The second graph in each set shows the<br />
estimates of the cost of each rem avoided.<br />
Several interesting conclusions can be deduced from these graphs:<br />
BWR reclrculatlon system decontaminations are more cost effective than P~R channel<br />
head decontaminations.<br />
The greatest net benefit is obtained from full system decontamination including<br />
the fuel. However, radwaste disposal costs make this the most expensive option.<br />
(Recent work suggests that radwaste costs might be significantly greater than the<br />
costs used in this study because they assumed resin bed efflclencles orlglnally<br />
are high.)