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

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4.24<br />

1) vitrification by in-can melting following spray calcination and 2) fluidized bed<br />

calcination. These processes are described in detail in DOE/ET-0028. They produce a<br />

borosilicate glass product and a granular powder product, respectively.<br />

Spray Calciner/In-Can Melting (Example Method)<br />

A flow diagram for the in-can melting process, the example high-level waste solidifica-<br />

tion process <strong>of</strong> this Statement, is shown in Figure 4.3.5. The liquid HLW is dried and cal-<br />

cined in a spray-calciner, the resultant calcine is mixed with about twice its weight <strong>of</strong><br />

glass-forming materials, and the mixture is melted within a steel canister. The filled can-<br />

ister is cooled and sealed by welding. The output <strong>of</strong> the example process amounts to about<br />

2.2 m 3 <strong>of</strong> waste glass per GWe-yr; higher volumes would result from lower waste loadings.<br />

The number <strong>of</strong> canisters used to contain this volume <strong>of</strong> glass depends on a number <strong>of</strong> factors,<br />

among which are the heat generation rate <strong>of</strong> the contained waste and the heat generation rate<br />

per canister allowed by disposal considerations. For canister heat loadings <strong>of</strong> 1.2 to<br />

3.2 kW (typical <strong>of</strong> those allowed in geologic repositories) and 6.5-year aged (out-<strong>of</strong>-<br />

reactor) waste, the number <strong>of</strong> canisters would amount to 44 and 17, respectively, per GWe-yr.<br />

A large variety <strong>of</strong> other glass-making processes have been developed; the output <strong>of</strong> these<br />

processes would be similar to that described here.<br />

Fluidized Bed Calcination<br />

In the fluidized bed calcination process (other calcination processes are also fea-<br />

sible), the liquid HLW is atomized as it enters the calciner vessel, which is heated by an<br />

in-bed combustion system. When the atomized HLW is injected into the hot bed, the waste<br />

constituents are converted to solids (primarily oxides) that adhere to the surface <strong>of</strong> par-<br />

ticles already in the bed. The bed is fluidized by heated air entering through perforations<br />

in the bottom support plate. Calcined product is removed continuously so that the bed<br />

AIR<br />

SPRAY CALCINER TOFF-GAS TREATMENT<br />

FRIT ADDITION<br />

FFILTERS<br />

STORAGE RACK<br />

DIVERTER r I I<br />

Si MDECONTAMINATION<br />

I STATION<br />

STATION<br />

FIGURE 4.3.5. Flow Diagram for Spray Calciner/In-Can Melting Process

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