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ANP lJHO JECT QUARTERLY PHOGRESS REPORT<br />

-. ~ .- ........<br />

TABLE 11.13. ANALYSIS OF CORROSIVE ATTACK BY SODIUM IN FIGURE 8 LQOP<br />

.<br />

~ __ ___.<br />

....... . __ ......... ....... ~ .____ .-..-.<br />

- .......... ____<br />

Heat exchanger<br />

section<br />

Hot section<br />

Cold section<br />

TEMPFmTURE<br />

(OF)<br />

1320<br />

1300<br />

1350<br />

1320<br />

750<br />

1100<br />

TIME<br />

(hr)<br />

2700<br />

1000<br />

2'100<br />

1000<br />

27 00<br />

1000<br />

were also continued in an effort to<br />

aid in <strong>the</strong> identification of <strong>the</strong><br />

corrosion products.<br />

Interaction of Fluorides urith<br />

Structural Netals (H. S. Powers, J. D.<br />

Redman, L. G. Overholser, Materials<br />

Chemistry Division). Investigation of<br />

<strong>the</strong> reaction of chromium and iron with<br />

molten NaF-KF-LiF eutectic has con-<br />

tinued. Special emphasis has been<br />

placed on <strong>the</strong> behavior of K2NaCrF6 and<br />

K2NaFeF6 when contacted with <strong>the</strong><br />

eutectic in <strong>the</strong> temperature range from<br />

600 to 1000°C. The filtrates col-<br />

lected at various temperatures in <strong>the</strong><br />

range from 500 to 800°C have been<br />

subjected to chemical analysis, as in<br />

<strong>the</strong> past, and <strong>the</strong> residues and filtrates<br />

have been examined by x-ray diffraction.<br />

In a number of experiments, 3 w t %<br />

of K2NaCrF6 was added to samples of<br />

<strong>the</strong> NaF-KF-LiF eutectic. The mixtures<br />

were heated at 800 to 1100°C under an<br />

atmosphere of helium for several hours<br />

and <strong>the</strong>n filtered at various teinpera-<br />

tures in <strong>the</strong> range from 500 to 800"C,<br />

and <strong>the</strong> residues and filtrates were<br />

examined. Heating of <strong>the</strong> K2NaCrF6 at<br />

temperatures up to 1100°C prior to its<br />

addition to <strong>the</strong> eutectic did not<br />

affect its solubility, and <strong>the</strong> temper-<br />

ature of equilibration of this compound<br />

with <strong>the</strong> eutectic prior to filtration<br />

was unimportant. Solubility was, how-<br />

ever, a function of temperature of<br />

filtration. The filtrate collected<br />

at 500°C contained 400 to 500 ppm Cr,<br />

whereas <strong>the</strong> filtrate obtained at ei<strong>the</strong>r<br />

152<br />

...<br />

2<br />

1<br />

2<br />

1<br />

2<br />

1<br />

ATTACK<br />

Occasional depressions, to 1 m il deep<br />

. -<br />

Numerous small depressions, to 0.25 mil deep<br />

No noticeable corrosion or erosion<br />

650 or 800°C contained 2000 to 3000<br />

ppm Cr. Microscopic examination re-<br />

vealed that most of <strong>the</strong> Cr was present<br />

as K2NaCrF6, which indicates that this<br />

compound is appreciably soliible in <strong>the</strong><br />

NaF-KF-LiF eutectic at elevated temper-<br />

atures. X-ray examination shows that<br />

in some runs, materials o<strong>the</strong>r than<br />

KzNaCrF6 have been present, including<br />

K,CrF6, Cr203, and KNaLiCrF,.<br />

Similar experiments in which Cr was<br />

added to <strong>the</strong> eutectic as metal instead<br />

of as K2NaCrFs showed that Cr20J, Cr,<br />

and K,NaCrF, were present after <strong>the</strong><br />

i n t e r a c t i on. Add i t ion a 1 p rod u c t s t ha t<br />

have not yet been identified were also<br />

found.<br />

A study of <strong>the</strong> solubility of K,NaFeF6<br />

in <strong>the</strong> NaF-KF-1iF eutectic and <strong>the</strong><br />

NaF-KF-LiF-UF,, mixture at 600 and<br />

800°C was made. It was found that with<br />

2.5% of K2NaFeF6 <strong>the</strong> solubility in<br />

both fluoride mixtures and at both<br />

temperatures of filtration was 6000 to<br />

7000 ppm. Apparently, all <strong>the</strong> K,NaFeF,<br />

added was dissolved.<br />

Since <strong>the</strong> presence of oxidation<br />

products in a number of <strong>the</strong> filtrates<br />

indicated that <strong>the</strong> digestion and<br />

filtration apparatus in which a blanket<br />

of helium is used does not exclude<br />

oxygen completely, two new types of<br />

reaction- fi ltration equipment have<br />

been designed and fabricated that<br />

should eliminate oxidative effects.<br />

Air Oxidation of Fuel Mixtures<br />

(R. P. Metcalf, F. F. Blankenship,<br />

Materials Chemistry Division). The

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