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ORNL-1771 - Oak Ridge National Laboratory

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Stability of Chrorni lam Compounds in<br />

Molten IF! uor ides<br />

J. D. Redinan C. F. Weaver<br />

Mater i al s Chem i s try Divi s ion<br />

It was shown in previous experiments that CrF,<br />

or some complex compound of divalent chromium<br />

was fhe corrosion product in the ZrFdobase fluoride<br />

melts of interest. However, when NaF-KF-LiF<br />

mixtures, with and without UF,, were tested in<br />

equipment prepared from al ley s containing chromium,<br />

the reaction products found were complex com-<br />

pounds of CrF,. Since films that were apparently<br />

NaK,CrF, or similar materials have been observed<br />

in some experiments, attempts have been made to<br />

observe the stability and soluLility of CrF, and<br />

CrF, in typical salt mixtures of the two types.<br />

In the temperature range 600 to 8RQ°C, CrF, is<br />

not stable in NaZrF, solution in contact with<br />

equipment of nickel. Examination of filtered speci-<br />

mens shows that the reaction<br />

2CrF, + Ni ,A NiF, + XrF,<br />

proceeds to essential completion, The solubility<br />

of 6rF2 in the NaZrF, solvent seems to exceed<br />

6000 parts of Cr per million parts of salt at 600%;<br />

solubility at 800°C seems ta be at least 15,000 ppm<br />

and may be consideratly higher.<br />

In the NaF-KF-LiF system it appears that CPF,<br />

is not stable. Whether the disproportionution re-<br />

action<br />

3CrF,-dCr0 i 2CrF,<br />

or some other mechanism is involved 15 not evident<br />

from the data available. It appears from preliminary<br />

evidence, however, that the solubility of Cr3' is<br />

several thousand parts per million at 600OC.<br />

Reduction of NiF, by H, in NaF-ZrF, Systems<br />

C. M. Blood H. A. Friedman<br />

G. M. Watson<br />

Materials Chemistry Division<br />

The use of hydrogen as a reducing agent in the<br />

removal of oxidizing impurities from fluoride melts<br />

has been routine for almost two years. One of the<br />

principal impurities removed is the Ni +' introduced<br />

as a result of treating the melts with hydrogen<br />

fluoride in nickel containers at 80OoC, Since<br />

hydrogen was first employed in this fashion, kinetic<br />

studies have been under way in order to supply data<br />

on which improved fluoride production procedures<br />

PERIOD ENDING SEPTEMBER 70, I954<br />

could be based. The Ni" was found to reduce so<br />

rapidly that the controlling step was the rate of<br />

removal of hydrogen fluoride from the melt; hence<br />

the chemistry of the process presents no problem of<br />

consequence from an engineering standpoint. With<br />

the completion of measurements at 800'C during the<br />

past quarter, these studies have been di scontinued.<br />

The experimentol method used for the measure-<br />

ments at 800°C was the same as that used in<br />

previously described experiments at 600 and<br />

?Oo°C.'8 Figure 5.5 shows a comparison of the<br />

effect of temperature on the rates of reduction for<br />

four concentrations. The slopes of the curves show<br />

that the apparent activation energy for the rate de-<br />

termining step is about 7800 cal, This energy of<br />

activation is in accord with the hypothesis that<br />

the reaction is heterogeneous and is catalyzed by<br />

nickei surfaces.<br />

18G. M. Wutsan, C. M. Blood, F. F. Rlankenship, ANP<br />

Quar, Prog, Reg). MUT. 10, 1954, QRNL-7692, p 62.<br />

____ ................. ...... ~-<br />

J .... .I ......... '<br />

fl~<br />

............. -<br />

~~ ..............<br />

A.-<br />

Fig. 5.5. Effect of Temperature and Concentra-<br />

tion on the Rate of Reduction of Nif, by H, in<br />

Molten NaF-ZrF1 (53-47 mole %).<br />

63

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