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ORNL-1816 - the Molten Salt Energy Technologies Web Site

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have been described in previous quarterly re-<br />

ports.21 Equilibrium data have been shown for<br />

<strong>the</strong> case in which <strong>the</strong> pure metals have served as<br />

<strong>the</strong> reducing agents and <strong>the</strong> solvent was NaZrF,.<br />

By application of identical techniques, ad-<br />

ditional data have been obtained on <strong>the</strong> UF,-Fe"<br />

reaction, for reduction of tiF, by Inconel, and<br />

for reactions of UF, with <strong>the</strong> pure metals in <strong>the</strong><br />

NaF-KF-LiF eutectic.<br />

The results of some additional studies on <strong>the</strong><br />

system<br />

Fe" + 2UF, = 2UF3 + FeF,<br />

in KaF-ZrF, at 600 and 8OOOC are given in Table<br />

5.3. In <strong>the</strong>se experiments, 2 g of hydrogen-fired<br />

iron wire was reacted with UF, in about 40 g of<br />

NaF-ZrF,. The values for Kx reported are defined<br />

as<br />

'6F- 'FeF,<br />

J L<br />

Kx = I<br />

C:F4<br />

where <strong>the</strong> concen tions are given in mole frac-<br />

tions with <strong>the</strong> NaF-ZrF, content considered as<br />

equal to 2 moles. The values for <strong>the</strong> UF, concen-<br />

,lJ. D. Redman and C. F. Weaver, ANP Qua7. Prog.<br />

Rep. Sept. 10, 19 -1771, p 60.<br />

TABLE 5.3. EQUILIBRIUM DATA FOR THE SYSTEM<br />

Fe" + 2UF4 = 2UF3 + FeFZ IN MOLTEN NaF-ZrF,<br />

AT 600 AND 8OO0C<br />

UF, Added: 0.360 mole/kg of melt<br />

C<br />

Fett in Filtrote<br />

*Blank of 100 ppm to be subtracted from determined<br />

values in calculations.<br />

PERIOD ENDING DECEMBER 'IO, 7954<br />

trations have been calculated from <strong>the</strong> Fett<br />

values found for <strong>the</strong> filtrates, since a reliable<br />

method for determining UF, in this mixture is not<br />

available.<br />

It will be noted that <strong>the</strong> values given for Kx<br />

at 600°C are larger than those at 8OO0C,. which<br />

is in agreement with all previous measurements.<br />

The values at <strong>the</strong> respective temperatures are<br />

also in fair agreement with those given earlier.<br />

The reaction between UF, and chromium in<br />

lnconel with NaF-ZrF, as solvent has been in-<br />

vestigated at 800°C. In <strong>the</strong>se experiments, 2 g<br />

of lnconel (hydrogen fired at 1200°C) WIJS con-<br />

tacted with <strong>the</strong> melt for 5 hr prior to filtration.<br />

The results are given in Table 5.4.<br />

The values given in Table 5.4 for <strong>the</strong> equi-<br />

librium constant are lower by about a iivefold<br />

factor than those obtained when chromium metal<br />

was used. It is possible that <strong>the</strong> activity of<br />

chromium metal in lncanel is appreciably less<br />

than its mole fraction. It appears more likely,<br />

however, that <strong>the</strong>se experiments represent "equi-<br />

librium" with lnconel whose surface layer is<br />

depleted of chromium metal. Additional data will<br />

be obtained by using longer equilibration times<br />

and varying surface-to-volume ratios.<br />

A study of equilibria for reactions of Fe" and<br />

Cr" with UF, in <strong>the</strong> NaF-KF-LiF eutectic has<br />

been started. It has been observed that when<br />

Fe" is equilibrated with <strong>the</strong> NaF-KF-LiF mixture<br />

alone about 100 ppm of Fe (presumably Fe") is<br />

found in <strong>the</strong> filtrate. This is very close to <strong>the</strong><br />

TABLE 5.4. DATA FBF! THE REACTION<br />

Cr (INCONEL) + 2UF4 = 2UF3 + CrFz AT 800°C IN<br />

MOLTEN NaF-ZrF,<br />

UF, Added: 0.360 mole/kg of melt<br />

**Activity of chromium in lnconel assumed to be equal<br />

to mole fraction (0.2).<br />

-5<br />

-5<br />

65

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