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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<strong>the</strong> salts are currently in essentially as pure<br />
condition as when charged into <strong>the</strong> reactor.<br />
Fuel <strong>Salt</strong><br />
MSRE runs 11 and 12 were completed within <strong>the</strong><br />
current report period During this period, small<br />
amounts of beryllium metal were dissolved into<br />
<strong>the</strong> fuel salt to adjust <strong>the</strong> oxidation-reduction<br />
potential of <strong>the</strong> salt. The total concentration of<br />
uranium in <strong>the</strong> fuel was also increased by addition<br />
of 7LiF-235UF, to <strong>the</strong> circulating salt Currently,<br />
<strong>the</strong> uranium concentration of <strong>the</strong> fuel salt is<br />
approximately 4 590 wt 76, of which <strong>the</strong> U3’ frac-<br />
tion of <strong>the</strong> total uranium is 1 5%. The effects of<br />
<strong>the</strong> beryllium and 7LiF-23sUF, additions are<br />
evident in <strong>the</strong> results of <strong>the</strong> chemical analyses of<br />
<strong>the</strong> fuel salt shown in Table 8 1. A refinement of<br />
analytical procedure was introduced during run 11;<br />
preliminary values for <strong>the</strong> determination of ura-<br />
nium concenttations were confirmed by a second<br />
group of analysts before final values were re-<br />
ported. Continuous control methods were em-<br />
ployed by both groups. This innovation in pro-<br />
cedure resulted in a significant improvement in<br />
precision. Average scatter was reduced from<br />
+0.5% to +0.4% of <strong>the</strong> value, corresponding to<br />
t0.03 and ‘0.02 wt % uranium.<br />
MSRE fuel salt is analyzed by IIF-H, purge<br />
methods €or evidence of oxide contamination. The<br />
results of analyses obtained during runs 11 and 12<br />
indicated that <strong>the</strong> fuel salt does not contain more<br />
than 50 to 60 ppm of oxide, that is, it is currently<br />
as free of oxide as when it was originally charged<br />
into <strong>the</strong> MSRE.<br />
Coolant <strong>Salt</strong><br />
When run 12 was terminated in August 1967, <strong>the</strong><br />
coolant salt had circulated in <strong>the</strong> MSRE for a<br />
period of 12,047 hr. Coolant salt specimens were<br />
submitted at onsmonth intervals during 1967.<br />
Results of those analyses show <strong>the</strong> composition<br />
and purity of <strong>the</strong> salt to be<br />
Li Be F Fe Cr Ni 0<br />
(wt W) (PPd<br />
___<br />
13.04 9.47 76.30 63 27 12 “’200<br />
103<br />
as compared with <strong>the</strong> composition and purity it<br />
was known to possess a year ago:<br />
Li Be F Fe Cr Ni 0<br />
.--.-<br />
(wt X) (PPd<br />
13.03 9.46 76.16 58 36 16 Q’200<br />
The two compositions are not differentiable with-<br />
in <strong>the</strong> precision of <strong>the</strong> analytic methods. The<br />
constancy of <strong>the</strong> trace concentrations of <strong>the</strong><br />
impurities attests to <strong>the</strong> fact that <strong>the</strong> cover gas,<br />
which is supplied to both <strong>the</strong> fuel and coolant<br />
circuits from a common source, has been main-<br />
tained in a state of high purity throughout tfie<br />
entire operational period.<br />
Flush Sait<br />
Whenever <strong>the</strong> MSRE fuel circuit is flushed with<br />
flush salt, <strong>the</strong>re is cross mixing uf fuel and flush<br />
salts by residues which remain in <strong>the</strong> reactor<br />
after each is drained. We need to know <strong>the</strong><br />
amounts of material transferred betwcen <strong>the</strong> fuel<br />
and flush salts because <strong>the</strong>y enter into <strong>the</strong> calcu-<br />
lation of <strong>the</strong> book-value concentration of uranium<br />
in <strong>the</strong> fuel salt. Sufficient analytical data are<br />
now available to enable us to deduce <strong>the</strong> average<br />
mass of <strong>the</strong>se rcsidues.<br />
The concentration of uranium in <strong>the</strong> flush salt<br />
appears to change in neatly equal increments<br />
during each flush operation, as shown in Table<br />
8.2. These data indicate that fuel salt which<br />
remains in <strong>the</strong> fuel circuit after drainage of <strong>the</strong><br />
fuel increases <strong>the</strong> uranium concentration of <strong>the</strong><br />
flush salt by 200 ppm each time <strong>the</strong> drained re-<br />
actor is cleaned with flush salt. An increase of<br />
200 ppm of uranium corresponds to <strong>the</strong> addition of<br />
approximately 850 g of uranium to <strong>the</strong> flush salt.<br />
This is <strong>the</strong> amount of uranium in 19.20 t 0.10 kg<br />
of fuel salt in which <strong>the</strong> uranium concentration is<br />
between 4 570 to 4 622 wt % U, <strong>the</strong> range for <strong>the</strong><br />
MSRE during <strong>the</strong> period considered.<br />
On filling <strong>the</strong> MSRE with fuel salt, 7L.iF-BeF2<br />
(66-34 mole %) flush salt residue is incorporated<br />
in <strong>the</strong> fuel salt, diluting its concentration of UF,<br />
and %rF4 slightly. This dilution is reflected in<br />
<strong>the</strong> uranium and zirconium analyses shown in Fig.<br />
8.1 The decrease in zirconium concentration of<br />
<strong>the</strong> fuel salt from a mean value of 11 33 wt % to<br />
10.85 wt ;“o corresponds to dilution of <strong>the</strong> fuel by<br />
12.7 kg of salt on each drain-flush-fill cycle.