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ORNL-TM-7207 - the Molten Salt Energy Technologies Web Site

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124<br />

large uncertainty is present in this estimate, of course, because of <strong>the</strong><br />

limited experience in decommissioning. However, <strong>the</strong> cost sf decommission-<br />

ing does not appear to be a large fraction of <strong>the</strong> cost of <strong>the</strong> construc-<br />

tion, and <strong>the</strong> present worth of expenditures to be made in <strong>the</strong> future is<br />

small. 'Fhe present worth of <strong>the</strong> estimated cost of decommissioning a DMSR<br />

40 years after start-up, discounted to <strong>the</strong> start-up date at a 4.5% dis-<br />

count factor, would be about $15 million.<br />

5.3*4 Fuel cvcle costs<br />

A% this stage of development and optimization of a ~n~e-through DMSR,<br />

several assumptions are necessary if a fuel cycle cost is to be estimated.<br />

One assumption 1s that <strong>the</strong> initial fuel charge will consist of 74<br />

mole 2 7LiF, 16.5 mole % BeF2, 8.23 mole 2 ThF4, and 1.27 mole X UF, plus<br />

UP3. If, as seems reasonable, an afkswanee is made for an additional 2%<br />

of molten fuel in <strong>the</strong> drain tank, <strong>the</strong> initial fuel solvent will require<br />

149 metric tons of ThF,, E13 metric tons of LiF, and 45.6 metric tons of<br />

BO2"<br />

quired; this is equivalent to 804 metric tons of U308 and would require<br />

8.05 x 105 swu for its enrichment.<br />

actor storage tank would consist of 33.1 metric tons (7.30 x ~ b 05 )<br />

material<br />

In addition, 23.5 metric tons of UP, enriched to 20% in 23% is re-<br />

Tke purified fuel delivered to <strong>the</strong> re-<br />

Total cost of <strong>the</strong> initial fuel is based on U308 at $35/lb, separative<br />

work at $SO/SWU, BeF2 at $15/lb, thorium at $15/kb Tho2$ and SLiF available<br />

at $3Jg of contained ki,<br />

* AII additional $2/lb of tetrafluoride has<br />

been allotted for conversion of Tho2 to n F4 and for CQrWerSiQn of UPg to<br />

UF$. The fuel, wade by mixing <strong>the</strong> powdered ingredients, must be purified<br />

in <strong>the</strong> molten state before use (as described in previous sections), Given<br />

<strong>the</strong> component fluorides at <strong>the</strong> prices above, <strong>the</strong> assunaption is that this<br />

purification can be performed for $$/lb of finished product.<br />

With <strong>the</strong>se assumptions, <strong>the</strong> total cost of <strong>the</strong> initial DMSR fuel<br />

charge is near $225 million (see Table 35). If we assme that <strong>the</strong> annual<br />

* his is <strong>the</strong> official price for small quantities of ~9,99+ a ~ i<br />

for<br />

use in PWRS. It is almost certainly too high (probably five-fold) if<br />

lithium were actually used in such quantities.

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