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ORNL-TM-7207 - the Molten Salt Energy Technologies Web Site

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surface.<br />

72<br />

Outgassing sf <strong>the</strong> moderator by pumping at reduces pressure and<br />

elevated temperature is necessary and sufficient to prevent contamination<br />

of <strong>the</strong> fuel by oxide ion from reactive gases from this source.<br />

Oxide films on <strong>the</strong> structural metal can also contaminate <strong>the</strong> fuel by<br />

oxide ion, and, as described previously, <strong>the</strong> dissolved ~e3+$ ~e2+$ and<br />

Ni2+ can be responsible for subsequent metal corr~sion.<br />

In operation sf<br />

<strong>the</strong> MSRE, <strong>the</strong> system was flushed with an LiF-BeF2 mixture for cleaning at<br />

start-up and after each shutdown before introduction of <strong>the</strong> fuel mixture.<br />

This precaution might be unnecessa%y, but it did suffice to keep oxide<br />

contamination caused by surface oxidation of <strong>the</strong> metal to a minimum.<br />

A small (-1OO-ppm) concentration of ~r2+ in <strong>the</strong> fuel as a consequence<br />

Of reaction Of <strong>the</strong> metal with <strong>the</strong> fuel Cartnot be aVOid@di. However, in <strong>the</strong><br />

absence of extraneous oxidants, <strong>the</strong> reacti~n is very slight, and <strong>the</strong> pres-<br />

ence Of Cr2' is CQIIIpbet@%y illlX3CuOuS.<br />

Grow-in of <strong>the</strong> fission products is also unavoidable, as is <strong>the</strong> pres-<br />

ence of a relatively small steady-state concentration of 3 ~ ~ .<br />

Atmsspherfc contamination. Reaction of <strong>the</strong> DMSK fuel mixture with<br />

*<br />

oxygen is relatively slow,<br />

but reaction with water vapor is more rapid,<br />

Fur<strong>the</strong>r, contaminati~n of <strong>the</strong> fuel with 40 to 50 ppm (by weight) sf oxide<br />

ion could result in precipitation of a uranium-rich (UTB%)02 solid SO~U-<br />

tion, A large ingress of contaminant air would be re~taired to produce<br />

40 ppm Of 02- in <strong>the</strong> fuel, and <strong>the</strong> DMSR would be designed amd operated SO<br />

as to minimize <strong>the</strong> chances sf such contamination. Operation of PISRE<br />

during much Of a fQuK'-yeaaP period With Illany ShUtdOWTls and several lrnimpor<br />

repair opera%ions sho~ed no evidence sf an increase in oxide contamina-<br />

tion level.22 ~reatment <strong>the</strong> initial fuel charge with anhydrous HF-B~<br />

mixture during its prepratton reataces <strong>the</strong> 02- concentration to innocuous<br />

Peve%s, and similar treatment of contaminated fuel would serve to re~~ve<br />

<strong>the</strong> o%-. such treatment might never be required, but in <strong>the</strong> DMSR, simple<br />

equipment should be included that is capable of treatment to ~emove oxide<br />

fOn should BnadVePtent CoRtPARinatiOn BCCUre<br />

dr<br />

KQW~V~P, <strong>the</strong> reactor metal at high temperature can readily react<br />

with oxygenB and <strong>the</strong> fuel can react with <strong>the</strong> oxides formed in this mannero<br />

.... . . . : .<br />

wx

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