ORNL-4191 - the Molten Salt Energy Technologies Web Site
ORNL-4191 - the Molten Salt Energy Technologies Web Site
ORNL-4191 - the Molten Salt Energy Technologies Web Site
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14.1 DETERMINAT1ON OF OXIDE<br />
IN MSRE SALTS<br />
R. F. Apple J. M. Dale<br />
A. S. Meyer<br />
During <strong>the</strong> last week of December <strong>the</strong> moisture-<br />
monitor cell in <strong>the</strong> oxide apparatus became inop-<br />
erative. Because of o<strong>the</strong>r experiments being<br />
performed in <strong>the</strong> same hot cell, <strong>the</strong> moisture-<br />
monitor cell was not replaced until March. The<br />
insensitive cell showed sortie superficial evidence<br />
of radiation damage in that <strong>the</strong> potting compound<br />
(an KTV preparation which is used to seal <strong>the</strong> tube<br />
containing <strong>the</strong> spiral electrodes in a stainless<br />
steel housing) had shrunk and cracked. Flow<br />
checks revealed that substantially all <strong>the</strong> flow was<br />
still passing through <strong>the</strong> electrolysis tube, so that<br />
<strong>the</strong> damage to <strong>the</strong> potting compound could not have<br />
been responsible for <strong>the</strong> cell failure. Resistance<br />
measurements indicated that <strong>the</strong> failure was<br />
caused by ei<strong>the</strong>r removal of or some alteration to<br />
<strong>the</strong> P,05 electrolyte film.<br />
The analyses of oxide in radioactive salt samples<br />
from <strong>the</strong> MSRE for this period are summarized in<br />
Table 14.1.<br />
Two samples of radioactive fuel (IPSL-19 and<br />
IPSL-24), submitted from <strong>the</strong> In-Pile <strong>Salt</strong> Loop 2,<br />
were found to contain 265 and 240 ppm of oxide<br />
respectively. Sample IPSL-24 was stored under<br />
helium at 200°C for a period of about six mont.hs<br />
from <strong>the</strong> time of sampling until <strong>the</strong> analysis was<br />
made.<br />
14.2 DETERMINATION OF U3'<br />
IN RADIOACTlVE FUEL BY A HYDROGEN<br />
REDUCTION METHOD<br />
J. RI. Dale R. F. Apple<br />
A. S. Meyer<br />
A transpiration method is currently being used<br />
to determine thc + 0 concentration in molten<br />
radioactive MSRE fuel. The molten fuel is sparged<br />
with hydrogen to reduce oxidized species according<br />
to fie reaction<br />
MFrl + --<br />
n in<br />
- H, -+ MF, + (n - RZ)IIF ,<br />
2<br />
167<br />
Table 14.1. Oxide Concentrations of MSRE <strong>Salt</strong> Somples<br />
Sample<br />
Dattt Received Oxide Concentration<br />
(PPd<br />
FP-11-28 (fuel) 3-2 1-67 58<br />
FP-12-4 (flush) 6-17-57 11<br />
FP-12-18 (fuel) 7-1 1-67 57<br />
The rate of production of HF is a function of <strong>the</strong><br />
ratio of oxidized to reduced species in <strong>the</strong> melt.<br />
The <strong>the</strong>ory of <strong>the</strong> method has been described pre-<br />
viously.<br />
The computer program which was under develop-<br />
ment has been completed and permits <strong>the</strong> calcula-<br />
tion of expected IIF yields for any preselected<br />
reduction steps on any melt composition. Using<br />
<strong>the</strong> present fuel composition and <strong>the</strong> experimental<br />
conditions of <strong>the</strong> transpirat ion experiment as input<br />
data to <strong>the</strong> program, €IF yields were calculated for<br />
varying initial concentrations of 1J3 '. Sample<br />
concentrations of U3' were determined from <strong>the</strong><br />
comparison of <strong>the</strong> experimental and calculated WF<br />
yields. Table 14.2 shows <strong>the</strong> U3+ results obtained<br />
from <strong>the</strong> [IF' yields of <strong>the</strong> third and fourth reduction<br />
steps of <strong>the</strong> analyses and compares <strong>the</strong>m with ex-<br />
pected values calculated by W. R. Grimes.<br />
The calculated results assume that 0.16% of <strong>the</strong><br />
uranium in <strong>the</strong> fuel was origiiially present as U3 ',<br />
that <strong>the</strong> chromium concentration increase from 38<br />
to 65 ppm which occurred before <strong>the</strong> first sample<br />
was taken resulted in <strong>the</strong> reduction of U4' to<br />
U3 ', that each fission event results in <strong>the</strong> oxida-<br />
tion of 0.8 atom of U3', and that <strong>the</strong>re have been no<br />
o<strong>the</strong>r losses of u3 '.<br />
It will be noted that no analysis results are<br />
listed for samples FP-11-38 and FP-11-49. Although<br />
<strong>the</strong>se samples were run in <strong>the</strong> normal manner, a<br />
total of over 2000 micromoles of HF was evolved<br />
for <strong>the</strong> four hydrogen reduction steps fox each<br />
sample as compared with about SS micromoles for<br />
<strong>the</strong> previous runs. Since this increased HF yield<br />
coincided with an increase in activity in <strong>the</strong> traps<br />
used to collect <strong>the</strong> HF, it appeared likely that <strong>the</strong><br />
buildup in sample activity during <strong>the</strong> extended<br />
period of reactor operation might be responsible.<br />
which 'J. M. Dale, K. 17. Apple, and A. S. Meyer, MSR<br />
"n may be UF,, NiF2' FeF2' CrF2y<br />
Proprarn Sernrmn. Pro&. Rrpf. f'cb. 28, 1967, C>&jL-<br />
UF4 in order of <strong>the</strong>ir observed reduction potentials. 4119, p. 158,