ORNL-1816 - the Molten Salt Energy Technologies Web Site
ORNL-1816 - the Molten Salt Energy Technologies Web Site
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 />
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