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PLENTIFUL ENERGY

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and residual sodium, all of which result in additional engineering challenges.<br />

Laboratory-scale demonstrations have been conducted at Marcoule in France,<br />

Dounreay in the U.K., and Tokai in Japan. A pilot scale project, TOR (5-10 T/yr),<br />

has been successfully demonstrated at Marcoule. It is clear that the same degree of<br />

economies of scale as contemplated for the LWR reprocessing plants cannot be<br />

achieved for the fast reactor processing plants with oxide fuel. Both the U.K. and<br />

France planned a 60 T/yr throughput rate as a target for the next set of pilot-scale<br />

plants.<br />

Further, remote fabrication of actinide-containing oxide fuel is extremely<br />

difficult. Uranium oxide fabrication is done currently with hands-on operation and<br />

requires precision milling of the pellets. Mixed oxide fabrication is done remotely,<br />

but maintenance also requires hands-on operation. Remotizing both fabrication and<br />

maintenance operations for actinide-containing fuels is a major challenge and<br />

would certainly sharply impact economics.<br />

On the hand, IFR metal fuel easily fabricates remotely using injection casting. It<br />

is compatible with pyroprocessing—both are compact processes. The two could<br />

make improvements in kind in the economics of fast reactor fuel cycle closure.<br />

Although many experts agree on the potential for improvements, exact<br />

quantification is a difficult task because of the difference in technology maturity.<br />

Aqueous reprocessing is much more fully developed, especially for LWR<br />

reprocessing. On the other hand, remote fabrication is better developed for metal<br />

than for oxide fuel. In addition to a large difference in the technology maturity<br />

level, the two processes are too radically different in all aspects to allow a direct<br />

comparison of one to the other.<br />

Conceptual designs for both, under the same ground rules, using a bottom-up<br />

approach, must first be developed. Credible estimates of capital costs can then be<br />

developed. Fortunately, comprehensive conceptual design efforts were carried out<br />

in the mid-1980s to allow such comparison. Argonne National Laboratory<br />

developed a detailed pre-conceptual design of commercial-scale fuel cycle facility<br />

based on pyroprocessing and metal fuel fabrication to serve a 1400 MWe fast<br />

reactor. [17] Oak Ridge National Laboratory and Hanford Engineering<br />

Development Laboratory jointly developed an equivalent fuel cycle facility based<br />

on aqueous reprocessing and mixed oxide fabrication to serve the same size reactor.<br />

[18]<br />

The pyroprocessing-based fuel cycle facility involves only a few processing<br />

steps, and all processing equipment systems are extraordinarily compact. There are<br />

dramatic simplifications and cost reductions in all three areas of reprocessing,<br />

refabrication, and waste treatment. The comparisons of these two facilities are<br />

summarized in Table 13-7.<br />

288

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