ORNL-2106 - the Molten Salt Energy Technologies Web Site
ORNL-2106 - the Molten Salt Energy Technologies Web Site
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