05.08.2013 Views

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

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.

<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.

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

Saved successfully!

Ooh no, something went wrong!