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ORNL-5388 - the Molten Salt Energy Technologies Web Site

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3-30<br />

The high alpha activity of uranium containing 232U will present two problems:<br />

1. In <strong>the</strong> UF, <strong>the</strong>re will be a strong (u,n) reaction. A crude estimate of <strong>the</strong> neutron<br />

emission from a 16-kg UF, product cylinder containing 0.6 wt% 23% is 5.7 x io7<br />

2.<br />

neutrons/sec at 10 days decay, 2.5 x lo8 at 30 days decay, and 8.7 x lo8 at 90 days<br />

decay.<br />

The 232U will provide a strong heat source in <strong>the</strong> UF, and <strong>the</strong> metal products. A<br />

crude estimate of <strong>the</strong> heat generation rate from pure 232U as a function of time after<br />

purification is: 0.03 W/g at 10 days, 0.13 W/g at 30 days, and 0.46 W/g at 90 days.<br />

The degree to which <strong>the</strong>se properties will affect weapon manufacture or delivery is<br />

unknown.<br />

Alternative Enrichment Arrangements to Reduce 232U Content in <strong>the</strong> Product. In considering<br />

<strong>the</strong> complications introduced to <strong>the</strong> final uranium metal product, i.e., <strong>the</strong> radiation<br />

level and heat generation resulting from 232U, it is apparent that removal of <strong>the</strong> 232U<br />

would be beneficial. Enrichment cascades can be designed to accomplish this. The most efficient<br />

arrangement would be to first design a cascade to strip 232U from all o<strong>the</strong>r uranium<br />

isotopes and <strong>the</strong>n to feed <strong>the</strong> tails from<br />

<strong>the</strong> first cascade to a second cascade where<br />

<strong>the</strong> fissile isotopes can be enriched. This<br />

Pmduct Containin<br />

Nearly All <strong>the</strong> 23%<br />

is illustrated in Fig. 3.3-2.<br />

c<br />

Uaste<br />

Fig. 3.3-2. Illustration of Enrichment<br />

Arrangement to Produce Low 232U Content<br />

Urani urn.<br />

Such an enrichment arrangement can be<br />

independent of <strong>the</strong> specific enriching device.<br />

Based on <strong>the</strong> discussion of <strong>the</strong> gas centrifuge<br />

process in Appendix A and at <strong>the</strong> beginning<br />

of this section, a small, low separative work<br />

capacity machine may be within <strong>the</strong> technical<br />

capabilities of a would-be diverter (see<br />

Appendix A).<br />

A1 though no information exists on <strong>the</strong><br />

separative work capacity of a Zippe machine<br />

in a cascade, a reasonable estimate of its<br />

separative capacity is about 0.3 kg SWU/yr<br />

when separating 235U from 238U.

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