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

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6.34<br />

be: (1) the pipe and valve manifold enclosure, (2) the condensing plant, and (3) gas pro-<br />

cessing equipment. Pipe and valve manifolding would be located in an enclosure near the top<br />

<strong>of</strong> the cavity operating shaft. The cooling water injected into the cavity and the steam from<br />

the cavity would be routed through this enclosure. There would be an operating and<br />

instrumentation gallery adjacent to the enclosure (Bechtel 1979a). (The HLLW would be<br />

charged through a separate underground pipe, mentioned above, that would not go through the<br />

confinement building or the pipe and valve manifold enclosure.)<br />

The condensing plant would cool and condense the steam coming out <strong>of</strong> the cavity and re-<br />

cycle it as cooling water during the waste charging phase. The potentially radioactive prim-<br />

ary cooling loop and the nonradioactive, closed-circuit intermediate cooling loop, along with<br />

the associated pumps and heat exchangers, would be shop fabricated in modules and designed<br />

for rapid remote maintenance. Since the rock would start to melt in a matter <strong>of</strong> days without<br />

cooling, all heat exchanger and pump systems would be designed and constructed with full re-<br />

dundant capacity to ensure constant cooling.<br />

Most <strong>of</strong> the gaseous elements in spent fuel would be removed during reprocessing at the<br />

fuel reprocessing facility. However, some fission product iodine in the liquid wastes could<br />

become volatile during the waste charging phase and would be carried out with the steam.<br />

This would be trapped by the gas processing equipment and returned with the cooling water to<br />

the waste charge or packaged for disposal in a mined geologic repository (Bechtel 1979a).<br />

Auxiliary facilities would support the systems and equipment located inside the con-<br />

finement building. These would include the water treatment plant, cooling tower, and<br />

radwaste treatment (Bechtel 1979a).<br />

Sealing Systems. There would be two principal shaft sealing operations:<br />

1. Sealing <strong>of</strong> the spare shaft after construction and before waste charging begins<br />

2. Sealing <strong>of</strong> the charging shaft after completion <strong>of</strong> waste filling but before rock<br />

melting begins.<br />

The NRC's Information Base for <strong>Waste</strong> Repository Design (NRC 1979) provides recommenda-<br />

tions for sealing conventional boreholes and shafts. Though this information base may not be<br />

particularly applicable to the rock melt concept, it states that removal <strong>of</strong> the steel casing<br />

is essential for long-term performance <strong>of</strong> the seal. The seal must be bonded directly to the<br />

geological strata for maximum strength. Expansive concretes make the best seals under cur-<br />

rent technology and do so at an acceptable cost. However, it is not certain that these<br />

seals, whether cement, chemical, or other material, will successfully resist deterio-<br />

ration over a period <strong>of</strong> 1,000 years on the basis <strong>of</strong> current penetration sealing technology.<br />

Seal failure must be assumed even for seals placed under carefully controlled conditions us-<br />

ing state-<strong>of</strong>-the-art technology and materials. Further development <strong>of</strong> sealing technology<br />

would, therefore, be required (DOE 1979).<br />

Postemplacement sealing <strong>of</strong> the pipes within the shaft, the shaft itself, and the pipes<br />

and valve gallery in the confinement building would be a more complex problem. This is be-

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