05.08.2013 Views

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

SHOW MORE
SHOW LESS

You also want an ePaper? Increase the reach of your titles

YUMPU automatically turns print PDFs into web optimized ePapers that Google loves.

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

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!