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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P<br />
as its chief impurity about 0.2 wt % sulfur. Purification<br />
of <strong>the</strong> RbF has proved to be difficult due to<br />
attack of <strong>the</strong> nickel purification equipment by <strong>the</strong><br />
sulfur. It has been found possible by rigorous HF<br />
5<br />
f and H, treatments to reduce <strong>the</strong> sulfur content to<br />
0<br />
- t<br />
.- %.<br />
an acceptable value, but in <strong>the</strong> process a large<br />
amount of nickel is picked up by <strong>the</strong> melt. Con-<br />
siderable treatment time is required to reduce <strong>the</strong><br />
resulting nickel fluoride so that it may be removed<br />
from <strong>the</strong> product.<br />
Preparation of Various Fluorides<br />
B. J. Sturm E. E. Ketchen<br />
structural metal fluorides and several complex<br />
from <strong>the</strong>se and alkali<br />
ed. These materials a<br />
fluorinated UF, are being utilized at increasing<br />
rates for various investigations of interest to <strong>the</strong><br />
ANP program. Chemical analysis, supplemented<br />
by x-ray and petrographic examination, has been<br />
utilized to determine purity and identity of <strong>the</strong><br />
materials.<br />
Uranium tetrafluoride, as received, may contain<br />
small amounts of oxides, moisture, and higher-<br />
ce uranium, Hydrofluorination at 6OOOC is<br />
carried out as a satisfactory method of re-<br />
P moving <strong>the</strong>se impurities. During <strong>the</strong> quarter, 11 kg<br />
of <strong>the</strong> purified material was supplied for studies<br />
requiring high-purity UF,. Additional batches of<br />
NiF, were prepared by <strong>the</strong> hydrofluorination at<br />
6OOOC of partially dehydrated NiCl ,*6H,O. Anhydrous<br />
AIF, was prepared by <strong>the</strong> <strong>the</strong>rmal de-<br />
c<br />
,.<br />
PERIOD ENDING DECEMBER 70,1954<br />
Fluorination of NiF,, CrF,, and FeF, has been<br />
discontinued because <strong>the</strong> analytical [methods<br />
available are not able to establish <strong>the</strong> fluorine-to-<br />
metal ratios accurately enough to determine <strong>the</strong><br />
effectiveness of <strong>the</strong> BrF, treatment in r'emoving<br />
small amounts of oxides that may be present.<br />
CHEMISTRY OF ALKALI HYDROXIDES<br />
L. G. Overholser F. Kertesz<br />
Materials Chemistry Division<br />
Purification of Hydroxides<br />
E. E. Ketchen<br />
Materials Chemistry Division<br />
Approximately 5 kg of NaOH was purified ei<strong>the</strong>r<br />
by filtering a 50 wt % aqueous solution through a<br />
fine sintered-glass filter or by decantinci a 50%<br />
solution to remove insoluble Na,CO,. 111 ei<strong>the</strong>r<br />
case <strong>the</strong> material was <strong>the</strong>n dehydrated at 400OC.<br />
Both methods produced material of desired purity<br />
(-0.1 wt % each of H,O and Na2C03). About<br />
1.8 kg of high-purity KOH (-0.1 wt % each K,CO,<br />
H,O, and Na) was prepared by reacting pure po-<br />
tassium with water, It is not planned to prepare<br />
more hydroxides in <strong>the</strong> near future because <strong>the</strong><br />
material on hand should supply <strong>the</strong> present limited<br />
requirements.<br />
Effect of Additives on Hydrogen Pressure<br />
Over NaOH-Ni System<br />
F. A. Knox<br />
Materia I s Chemistry Di vis ion<br />
The effects of small additions of NiO, Na,O,<br />
and mixtures of <strong>the</strong> two on <strong>the</strong> hydrogen pressure<br />
by using a modification rev i ou s I y desc r i bed<br />
<strong>the</strong> formation of<br />
Three batches of FeF, were fluorinated as a<br />
,,ANP Quar. Prog. Rep. Sept. 10, 1953, <strong>ORNL</strong>-1609,<br />
means of removing small amounts of impurities. p 84.<br />
71