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ORNL-1816 - the Molten Salt Energy Technologies Web Site

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ru<strong>the</strong>nium was apparently volatilized out of <strong>the</strong><br />

reactor entirely. Ru<strong>the</strong>nium and niobium plated<br />

out heavily on <strong>the</strong> metal walls of <strong>the</strong> reactor. The<br />

distribution ratio between metal wall and salt was<br />

about 5 for ru<strong>the</strong>nium activity and less than 0.01<br />

for niobium activity.<br />

The behavior of plutonium in <strong>the</strong> fused salt<br />

fluoride-volatil ity process is important in processing<br />

fuel that has a high proportion of U238. The<br />

results of many fluorination runs at 650°C show<br />

that only about 0.01% of <strong>the</strong> plutonium is carried<br />

over with <strong>the</strong> UF, product.<br />

Fur<strong>the</strong>r study was carried out on <strong>the</strong> absorption<br />

of UF, in NaF-ZrF, (56-44 mole %) at 65OOC.<br />

In one trial, 9 g of UF, was absorbed in 30 g of<br />

NaF-ZrF, in 1 hr with no noticeable loss. However,<br />

passage of helium through <strong>the</strong> fused salt,<br />

ei<strong>the</strong>r concurrently with or after <strong>the</strong> UF, addition,<br />

erable fuming. A positive test for<br />

fluorine with potassium iodide paper was obtained,<br />

which indicated reduction of <strong>the</strong> adsorbed UF, to<br />

<strong>the</strong> tetra- or pentavalent form of uranium. A<br />

gravimetric test, based on <strong>the</strong> reaction of fluorine<br />

with sodium chloride, showed that <strong>the</strong> breakdown<br />

of UF, to F, and UF, amounts to 1 to 2% per hour<br />

at 65OOC.<br />

Engineering information is needed on two steps<br />

in <strong>the</strong> fluoride-volatility process: fluorination and<br />

,. UF, cold-trapping. Effective contacting of fluorine<br />

with molten ARE fuel is desirable to minimize<br />

fluorine consumption and gaseous waste and to<br />

assure complete recovery of <strong>the</strong> uranium. The cold<br />

trap should be operated in such a manner that all<br />

<strong>the</strong> UF, will be condensed and collected on <strong>the</strong><br />

PERIOD ENDING DECEMBER 70,7954<br />

properties of <strong>the</strong> liquid could not be demonstrated<br />

by a simple correlation of friction factor with<br />

Reynolds number, such as is found in ordinary<br />

fluid flow through pipes. The acetylerie tetra-<br />

bromide studies showed that vertical mixirig of <strong>the</strong><br />

liquid phase was induced by a gas rate of 9.5 cfm<br />

in a 12-in.-dia column. Equipment is now being<br />

assembled to verify <strong>the</strong>se conclusions with molten<br />

Na F-Z r F ,.<br />

Cold traps to be used for a quantitative study<br />

of <strong>the</strong> effect of temperature and gas flow rate on<br />

<strong>the</strong> completeness of UF, removal are being con-<br />

structed. The design of <strong>the</strong>se traps is based on a<br />

K-25 cold-trap design.<br />

APPLICATIONS OF FUSED SALT-VOLATILITY<br />

PROCESSES<br />

A long-range study has been made to survey <strong>the</strong><br />

over-all feasibility of fused salt-voIatiIi,ty tech-<br />

niques in <strong>the</strong> chemical processing of ARE-type<br />

reactor fuels and certain types of heterogeneous<br />

reactor fuel elements. The volumes of raclioactive<br />

waste from such processes should be mulch lower<br />

than those from <strong>the</strong> aqueous processes, and<br />

processing costs should be low, even though a<br />

means of disposing of excess fluorine will have<br />

to be provided. Total chemical costs, ?which in<br />

present aqueous processes represent approximately<br />

10% of operating costs, have been estimated to be<br />

20g per gram of U235. The operational procedure<br />

is much simpler, and <strong>the</strong> equipment should be<br />

inexpensive, even though nickel will be required<br />

as <strong>the</strong> material of construction.<br />

Results of recent work on fuel element dissolution<br />

137

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