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ANP PROJECT QIJARTERX,Y PRQCRESS REPORT<br />

mixture intimately mixed. The capsule<br />

is <strong>the</strong>n tilted so that <strong>the</strong> ball closes<br />

<strong>the</strong> lower valve and isolates <strong>the</strong> upper<br />

part of <strong>the</strong> salt phase, which is <strong>the</strong>n<br />

solidified 2nd analyzed for its<br />

potassium content. The data obtained<br />

are summarized in Table 10.4.<br />

PRODUCTION AND PURIFICATION OF<br />

FLUORIDE MIXTURES<br />

F. F. Blankenship G. J. Nessle<br />

Materials Chemistry Division<br />

IJse of <strong>the</strong> hydrogenation-hydro-<br />

fluorination process previously<br />

described for fuel-sample preparation<br />

has been continued on laboratory and<br />

pilot scales for production of standard<br />

materials for corrosion testing,<br />

physical property evaluat,ion, and<br />

1 arge -component t es t ing .<br />

Construction of <strong>the</strong> production<br />

equipment to furnish 3000 lb of NaZrFS<br />

for <strong>the</strong> ARE is in an advanced stage.<br />

Raw materials are being accumulated at<br />

a satisfactory rate.<br />

A modification of <strong>the</strong> purification<br />

treatment has been adopted for micro-<br />

scale processing of samples containing<br />

enriched uranium for radiation-damage<br />

testing.<br />

Aslight modification of <strong>the</strong> standard<br />

procedure has been used successfully<br />

to purify mixtures containing 50<br />

mole % NaF, 25 mole % ZrF4, and 25<br />

mole % UF,.<br />

Preparation of NaZrF5 by direct<br />

hydrofluorination of ZrO, in <strong>the</strong><br />

presence of NaF has been moderately<br />

successful in simple equipnien t. Fur<strong>the</strong>r<br />

study of this process is planned.<br />

-<br />

122<br />

Labor at0 ry - Sc a1 e Foe 1 P reparation<br />

(13. E. Thoma, C. M. Blood, F. P. Boody,<br />

Materials Chemistry Division) . Fourteen<br />

batches of purified molten fluoride<br />

compositions, both coolant and fuel,<br />

have been prepared for loop tests,<br />

measurement of physical properties,<br />

and corrosion testing. These were<br />

treated in essentially <strong>the</strong> same manner<br />

as previously reported.(")<br />

To explore <strong>the</strong> unlikely possibility<br />

that hydrogen reduces UF, or ZrF,,<br />

two of <strong>the</strong> fuel batches were given an<br />

additional hydrogenation for 1 hr<br />

following <strong>the</strong> regular procedure. No<br />

evidence of reduced phases in <strong>the</strong><br />

products from <strong>the</strong>se runs was shown by<br />

examination with <strong>the</strong> petrographic<br />

microscope. However <strong>the</strong>re is evidence<br />

that <strong>the</strong> material so prepared was<br />

slightly less corrosive in small-scale<br />

tests than was <strong>the</strong> standard fuel. No<br />

explanation for this effect has been<br />

suggested; however, fur<strong>the</strong>r study of<br />

this behavior is planned.<br />

Modifications of techniques of<br />

assembling and disassembling apparatus<br />

have resulted in less frequent failure<br />

than was experienced at <strong>the</strong> beginning<br />

of <strong>the</strong> hydrofluorination program.<br />

Corrosion of <strong>the</strong> reactors has not yet<br />

been a problem when <strong>the</strong> standard<br />

treatment is applied to relatively<br />

pure fluoride mixtures.<br />

Pilot-Scale Fuel Purification<br />

(G. J. Nessle, J. E. Eorgan, Materials<br />

Chemistry Division). Two apparatus<br />

capable of producing up to 3 kg of<br />

('"C. M. Blood, F. P. Boody, A. J. Weinberger,<br />

and G. J. Nessle, ANP Quar. Prog. Rep. June 10.<br />

1952, ORNL-1294, p. 97.<br />

TABLE 10.4. SOLUBILITY OF POTASSIUM IN NaF-KF-LiF<br />

........ ._._____-<br />

_.<br />

TEMPERATURE OF NO. OF<br />

POTASSIUM CONTENT<br />

EXPERIMENT (OC) E XP En I ME NT S<br />

(mol@ %)<br />

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

544<br />

68 6<br />

9 20<br />

10 40<br />

....... 1<br />

I L<br />

.... ......... ._-I.<br />

3.8<br />

3. 5<br />

3.7 * 0.5<br />

3.9

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