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Management of Commercially Generated Radioactive Waste - U.S. ...

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4.39<br />

The packaged waste output <strong>of</strong> the cementation systems depends markedly on whether or not<br />

the combustible wastes are incinerated (because the incinerator ash and scrubber solutions<br />

are additional feeds to the cementation systems). If the combustible wastes are inciner-<br />

ated, the output <strong>of</strong> the cementation systems will be 106 55-gallon drums/GWe-yr at an FRP and<br />

31 55-gallon drums/GWe-yr at a MOX-FFP. About 40% <strong>of</strong> the drums originating at an FRP and<br />

all <strong>of</strong> the drums originating at a MOX-FFP could be contact-handled.<br />

If the combustible wastes are not incinerated, the packaged waste output <strong>of</strong> the cemen-<br />

tation systems will be 49 55-gallon drums/GWe-yr at an FRP and 11 55-gallon drums/GWe-yr at<br />

a MOX-FFP. All <strong>of</strong> the drums originating at an FRP require remote handling, but those origi-<br />

nating at a MOX-FFP would be contact-handled.<br />

Bitumenization<br />

Imnobilization <strong>of</strong> radioactive wet wastes in bitumen involves mixing the waste with<br />

liquid bitumen or asphalt binder and placing it in 55-gallon drums. The temperature <strong>of</strong> the<br />

binder at the time <strong>of</strong> mixing (above 100 0 C) evaporates the free water, and thus reduces the<br />

waste volume. Use <strong>of</strong> bitumen to immobilize radioactive wastes has been well demonstrated,<br />

largely through extensive operating experience in Europe. However, it is uncertain whether<br />

bitumenized waste forms will meet waste form criteria for repositories.<br />

Several types <strong>of</strong> bitumenization processes have been developed as discussed in<br />

ERDA-76-43. In this Statement, a continuous screw extruder process was considered for the<br />

following reasons:<br />

* The screw extruder bitumenization process operates at lower temperatures and with<br />

shorter residence times than the batch process, thus minimizing <strong>of</strong>f-gas problems.<br />

* The process uses well-demonstrated technology.<br />

* The process is commercially available in the U.S.<br />

A process flow diagram for a bitumenization system at an FRP is shown in Figure 4.3.11.<br />

A similar system can be used at a MOX-FFP after neutralization <strong>of</strong> acidic liquids.<br />

If the combustible wastes are incinerated, the packaged waste output <strong>of</strong> the bitumeniza-<br />

tion systems will be 48 55-gallon drums/GWe-yr at an FRP and 10 55-gallon drums/GWe-yr at a<br />

MOX-FFP. About 2% <strong>of</strong> the drums originating at an FRP and all <strong>of</strong> the drums originating at a<br />

MOX-FFP could be contact-handled.<br />

If the combustible wastes are not incinerated, the packaged waste output <strong>of</strong> the bitu-<br />

menization systems will be 26 55-gallon drums/GWe-yr at an FRP and 8.7 55-gallon drums/<br />

GWe-yr at a MOX-FFP. About 3% <strong>of</strong> the drums originating at an FRP and all <strong>of</strong> those originat-<br />

ing at a MOX-FFP could be contact-handled.<br />

4.3.4 Gaseous and Airborne <strong>Waste</strong> Treatment<br />

Spent nuclear fuel contains some radionuclides that are released in gaseous form during<br />

certain treatment operations. Such volatile radionuclides include the fission products<br />

H, 85 Kr, and 129I and the activation product 1C. A small portion <strong>of</strong> the fission product

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