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ORNL-2106 - the Molten Salt Energy Technologies Web Site

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ANP PROJECT PROGRESS REPORT<br />

fixed midway between <strong>the</strong> two half cells was<br />

formerly used as <strong>the</strong> cell temperature. In order to<br />

refine <strong>the</strong> temperature measurements, a calibrated<br />

<strong>the</strong>rmocouple, enclosed in a nickel tube, was sub<br />

stituted for an electrode in a dummy cell. In <strong>the</strong><br />

temperature range of interest (550 to 750OC) <strong>the</strong><br />

melt temperatures found were 10 f 2OC higher than<br />

<strong>the</strong> melt temperatures at <strong>the</strong> center between <strong>the</strong> two<br />

crucibles. Thus all <strong>the</strong> temperatures reported in<br />

connection with previous potential measurements<br />

should be revised upward by 10°C. Only <strong>the</strong> solu-<br />

bility data are sufficiently temperature sensitive<br />

to be appreciably affected.<br />

Application of <strong>the</strong> temperature correction to <strong>the</strong><br />

solubility data previously reported' gave <strong>the</strong><br />

following new expressions for <strong>the</strong> solubility of<br />

MF,.ZrF, in NaF-ZrF, (53-47 mole %):<br />

36.0~ 103<br />

IogN = - + 6.87 , for FeF,*ZrF,<br />

4.576 T<br />

40.1 103<br />

log N = - + 8.36 , for CrF,*ZrF,,<br />

4.576 T<br />

28.8 103<br />

109 N = - + 4.72 , for NiF,.tF,,16<br />

4.576 T<br />

where N is <strong>the</strong> mole fraction of MF2*ZrF4 and T is<br />

temperature in OK. The corrected heats of solution<br />

and "ideal" melting points are now 36.0, 40.1, and<br />

28.8kcal/mole MF,.ZrF, and 875, 775, and 1060OC<br />

for <strong>the</strong> Fe, G, and Ni compounds, respectively.<br />

Solubility data obtained by analyses of filtrates<br />

from saturated solutions, as described in <strong>the</strong> pre-<br />

ceding sections of this chapter ("Equilibrium<br />

Reduction of NiF, by H, in NaF-ZrF," and 'lSolu-<br />

bility and Stability of Structural Metal Fluorides in<br />

<strong>Molten</strong> NaF-ZrF,"), did not agree with <strong>the</strong> elec-<br />

trometr ica I I y determined so I ubi I i<br />

t ies, particular I y<br />

in <strong>the</strong> case of NiF,. Since <strong>the</strong> filtration measure-<br />

ments were carried out by adding NiF, ra<strong>the</strong>r-than<br />

NiF,.tF, as solute (and similarly with FeF, and<br />

Cr F,), <strong>the</strong> electrometric determinations were re-<br />

peated with NiF, as solute so that <strong>the</strong> data could<br />

16From this investigation and x-ray and petrographic<br />

examinations of quenches of NaF-ZrF4 melts, NiF, is<br />

now believed to exist in a ternary compound, ra<strong>the</strong>r than<br />

as NiF2*ZrF4, in saturated solutions. The equation<br />

for <strong>the</strong> solubility was revised to include additional<br />

measurements, as well as <strong>the</strong> temperature correction.<br />

104<br />

be compared. X-ray and petrographic examinations<br />

of <strong>the</strong> solidified melt from <strong>the</strong> half cells should<br />

have sufficed to identify ei<strong>the</strong>r or both of <strong>the</strong> joins<br />

W<br />

as quasi-binary; in practice, however, both<br />

NiF,*ZrF, and a new phase were found in <strong>the</strong><br />

slowly cooled half cells. The new phase is thought<br />

to be a ternary compound, since it has never been<br />

found in <strong>the</strong> binary systems.<br />

Gradient quenches (510 to 540°C) along <strong>the</strong> two<br />

joins revealed only <strong>the</strong> new phase, with no<br />

NiF,*EF,. Such ambiguous results were disappointing,<br />

since on a quasi-binary join <strong>the</strong> solubility<br />

does not vary with <strong>the</strong> amount of solute<br />

added, as it does along a random join.<br />

Cells containing MF, in NaF-ZrF, (53-47 mole<br />

%), with no addition of ZrF,, gave <strong>the</strong> solubilities<br />

of <strong>the</strong> structural metal salts shown in Table 2.2.10<br />

and Fig. 2.2.4 for NiF, and Table 2.2.11 for FeF,.<br />

The solubilities of <strong>the</strong> nickel salts along <strong>the</strong> joins<br />

NiF2eZrF4-7NaF*6ZrF4 and Ni F2-7NaF*6ZrF4, as<br />

well as <strong>the</strong> values for NiF, obtained by filtration<br />

methods, are plotted in Fig, 2.2.4. The discrepancy<br />

between <strong>the</strong> results of <strong>the</strong> various experiments<br />

has not been explained. The electrometrically<br />

determined solubilities appear to be virtually <strong>the</strong><br />

some whe<strong>the</strong>r <strong>the</strong> solute is added as NiF, or as<br />

NiF,*tF,, and <strong>the</strong> same seems to be true for<br />

TABLE 2.2.10. SOLUBILITY OF NiF, IN<br />

NaF-ZrF, (53-47 MOLE %)<br />

&fsoln = 28.8 kcal<br />

Ideal melting paint = 106OoC<br />

Temperature NiF, Solubility<br />

(OC) wt % mole %<br />

553 0.12 0.12<br />

564<br />

0.14 0.15<br />

1<br />

574 0.19 0.20<br />

576 0.20 0.21<br />

650 0.79 0.83<br />

650 0.93 0.97<br />

655 0.88 0.92<br />

669 0.98 1.01<br />

706 1.97 2.0 5<br />

725 2.19 2.29<br />

i

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