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ORNL-5388 - the Molten Salt Energy Technologies Web Site

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e<br />

A-10<br />

technique is that a module, de'fined as a separation unit consisting of one set of com-<br />

pressors and one set of separation elements, does not as in <strong>the</strong> classic case, produce only<br />

one separation factor of enrichment in one pass but can produce for a constant separative<br />

work capacity various degrees of enrichment up to a maximum of several times <strong>the</strong> separation<br />

factor over <strong>the</strong> element.<br />

Full scale modules of this type are nearing <strong>the</strong> prototype stage. Recent design<br />

improvements are expected to result in a nominal capacity of 80 to 90 kg SWU/yrll per<br />

separation module.<br />

A valuable feature of a plant based on this process is its very low uranium inven-<br />

tory, which results in a short cascade equilibrium time, of <strong>the</strong> order of 16 hours for a<br />

commercial plant enriching uranium to 3% 235U.<br />

The <strong>the</strong>oretical lower limit to <strong>the</strong> specific energy consumption of <strong>the</strong> separation<br />

element can be shown to be about 0.30 MW.h/kg SW. The minimum figure observed by <strong>the</strong><br />

developers with laboratory separating elements is about 1.80 MW.h/kg SW, based on<br />

adiabatic compression and ignoring all system inefficiencies. This difference is a<br />

measure of <strong>the</strong> improvement potential expected by <strong>the</strong> South Africans.<br />

Current and Projected Enrichment Capacity<br />

Most of <strong>the</strong> known installed enrichment capacity is based upon gaseous diffusion<br />

technology. Only small increments of centrifuge technology are in operation (1 .e. ,<br />

URENCO, Japan and U.S.), and one plant utilizing modified nozzle technology (<strong>the</strong> South<br />

African Helikon plant) may be operating. Indicative of <strong>the</strong> status of o<strong>the</strong>r isotope<br />

separation methods, all planned additions to <strong>the</strong> world enrichment capacity are based on<br />

ei<strong>the</strong>r diffusion, centrifuge or nozzle technology.<br />

The existing worldwide capacity and planned additions to capacity are shown in<br />

Table A-1 by colcntry and technology type. In <strong>the</strong> table <strong>the</strong> groups identified as<br />

Eurodif and Coredif are multinational organizations building gaseous diffusion plants<br />

in France.<br />

A.2, New Separation <strong>Technologies</strong><br />

In addition to <strong>the</strong> more developed technologies (gaseous diffusion, gas centri-<br />

fuge, and <strong>the</strong> Becker nozzle), <strong>the</strong>re are several o<strong>the</strong>r separation methods that ei<strong>the</strong>r<br />

have been utilized in <strong>the</strong> past or are currently being developed. These technologies<br />

are listed in Table A-2.<br />

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