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ORNL-1816 - the Molten Salt Energy Technologies Web Site

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1Y PROGRESS REPORT<br />

y equilibration of Fe" with NaZrF,<br />

in similar equipment. However, equilibration of<br />

Cr" with <strong>the</strong> alkali fluoride eutectic produces<br />

about 500 ppm of Cr in solution, and, based on<br />

<strong>the</strong> findings reported in <strong>the</strong> preceding section,<br />

this is, presumably, a mixture of Cr3' and Cr".<br />

This high concentration of soluble chromium in<br />

<strong>the</strong> NaF-KF-LiF system is surprising, since about<br />

100 ppm of Crtt is obtained in a similar equilibration'<br />

with NaZrF,. The reaction responsible<br />

st<br />

value is not yet known.<br />

for <strong>the</strong> reaction of UF, with<br />

olvent indicate that at 300°C about<br />

s present in <strong>the</strong> equilibrium<br />

filtrate; this is nearly <strong>the</strong> same concentration<br />

. At 6OO0C, however, about<br />

covered in <strong>the</strong> filtrate. It<br />

that <strong>the</strong> complex reaction in<br />

h more temperature sensitive<br />

e reaction in NaZrF,.<br />

PRODUCTION OF PURIFIED MOLTEN<br />

FLUORIDES<br />

F. F. Blankenship G. J. Nessle<br />

L. G. Overholser<br />

Materials Chemistry Division<br />

Electrolytic Purification of Zirconium-Base<br />

Fluorides<br />

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

F. W. Miles F. P. Boody<br />

Materials Chemistry Division<br />

Interest in <strong>the</strong> extremely short process time and<br />

high efficiency obtained in <strong>the</strong> electrolytic purifi-<br />

cation of molten NaF-ZrF, mixtures led to an ex-<br />

ploration of <strong>the</strong> limitations of electrolysis as a<br />

means of purification. At cathode current densities<br />

up to 0.3 amp/cm2, <strong>the</strong> presence of UF, in a salt<br />

mixture was found to greatly reduce <strong>the</strong> efficiency<br />

of electrolysis because <strong>the</strong> reduction of UF, to<br />

at <strong>the</strong> cathode was counteracted by <strong>the</strong><br />

UF,<br />

oxidation of UF, to UF at <strong>the</strong> anode. A steady<br />

state was approached wten about 5% of <strong>the</strong> UF,<br />

had been converted to UF,. Apparently <strong>the</strong> rapid<br />

NaF-ZrF, mixtures cone,<br />

in large part, to <strong>the</strong><br />

of zirconium metal on<br />

removal of fluorine as HF<br />

<strong>the</strong> stripping gas or as<br />

was used. The reduced<br />

e precipitated in <strong>the</strong><br />

cathode deposit. Any structural metal ions which<br />

were not deposited as a primary electrode process<br />

were precipitated by reaction with <strong>the</strong> zirconium<br />

metal.<br />

Electrolysis was most effective in purification<br />

when two advantages were achieved: first, a rapid<br />

rate of over-all reduction of <strong>the</strong> melt, or a good<br />

current efficiency, as measured by a high rate<br />

of removal of HF or fluorocarbons, and second,<br />

<strong>the</strong> deposition of impurities as an adherent cathode<br />

coat which could be removed from <strong>the</strong> cell. In<br />

NaF-Li F-KF mixtures <strong>the</strong> electrolytically reduced<br />

potassium was slightly soluble in <strong>the</strong> melt, and<br />

<strong>the</strong>refore oxidation of dissolved potassium at <strong>the</strong><br />

anode nullified reduction at <strong>the</strong> cathode and <strong>the</strong><br />

current efficiency for over-all reduction was low.<br />

Also, an adherent cathode deposit was not<br />

regularly found. Presumably, both <strong>the</strong>se ad-<br />

vantages could be regained, not only for <strong>the</strong><br />

NaF-LiF-KF system but for UF4-containing melts<br />

as well, by alterations in cell design, electrode<br />

construction, and current densities.<br />

Some of <strong>the</strong> incidental points noted were that<br />

0-- and SO,-- could be removed by electrolysis<br />

in NaF-ZrF, melts, and hence HF treatment is<br />

not necessarily required in <strong>the</strong> purification of salt<br />

mixtures. Platinum was unsuitable as an anode<br />

material. The NaF-LiF-KF mixtures were par-<br />

ticularly prone to show an "anode effect," or gas<br />

polarization of <strong>the</strong> graphite anode, when <strong>the</strong>re<br />

was a slight contamination by air. The UF,-UF,<br />

oxidation-reduction system showed no polarization<br />

at graphite anodes or nickel cathodes.<br />

The electrolyses were carried out in apparatus<br />

of <strong>the</strong> type previously described.22 The graphite<br />

anodes were 1.12 cm in diameter and were im-<br />

mersed to a depth of about 10 cm to give an area<br />

of about 25 cm2. The cathodes were constructed<br />

of a ?-in.-dia cylinder of nickel gauze having a<br />

8<br />

calculated immersed area of about 70 cm2. The<br />

wet areas of <strong>the</strong> pot and of <strong>the</strong> probes which were<br />

occasionally used as electrodes were 500 and<br />

10 cm2, respectively. Ordinarily, 10 amp was<br />

passed during any continuous electrolysis step.<br />

Preliminary results with SO,-- removal were<br />

sufficiently encouraging that an electrolysis trial<br />

with helium as <strong>the</strong> sweep gas was carried out on<br />

a 3-kg batch of KaF-ZrF, (53-47 mole %) which<br />

had received no previous purification o<strong>the</strong>r than<br />

me<br />

LL C. M. Blood et al., ANP Quar. Prog. Rep. Sept. 10.<br />

1954, <strong>ORNL</strong>-1771, p 73.<br />

t<br />

P

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