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ANP PRQ JECT QUARTERLY PROGRESS RQEO<br />
times when high urani urn conc en tra tioris<br />
are used.<br />
A test was run in <strong>the</strong> tilting<br />
furnace under standard conditions of<br />
time and temperature with NaF-ZrF4-UF,<br />
(50-46-4 mole %) that had been treated<br />
with hydrogen after purification by<br />
<strong>the</strong> norma 1 hydrogena tion-hydro fluor i -<br />
nation method. Type 316 stainless<br />
steel showed somewhat less attack when<br />
subjected to <strong>the</strong> hydrogen-treated<br />
material than when exposed to material<br />
prepared in <strong>the</strong> standard fashion. The<br />
Inconel tubes were found to be lightly<br />
attacked (0.5- to 1-mil penetration)<br />
when in contact with <strong>the</strong> hydrofluorin-<br />
ated material, but <strong>the</strong>y evidenced no<br />
atthck when exposed to <strong>the</strong> hydrogen-<br />
treated material. These preliminary<br />
tests indicate that a final hydrogen<br />
treatment of <strong>the</strong> fuel would be bene-<br />
ficial. Additional tests are scheduled.<br />
Temperature Dependence. Although<br />
<strong>the</strong> immediate application of <strong>the</strong><br />
fluoride fuel NaF-ZrF4 -UF, (50-46-4<br />
mole %) is to be limited t.0 a tempera-<br />
ture of 1500"FJ some corrosion tests<br />
under static conditions were performed<br />
at considerdbly higher temperatures to<br />
determine <strong>the</strong> temperature-dependence<br />
of <strong>the</strong> corrosiveness of this fuel. As<br />
<strong>the</strong> data in Table 11.5 indicate,<br />
penetration of <strong>the</strong> Inconel by <strong>the</strong><br />
fluorides in <strong>the</strong>se 100 hr tests in-<br />
creased slightly, if at all, over <strong>the</strong><br />
ternperaturc range 800 to 1200°C.<br />
It is interesting to note that<br />
Inconel seems to lose weight at 1200°C<br />
instead of gaining weight as is usual<br />
at <strong>the</strong> lower temperatures. No expla-<br />
nation for <strong>the</strong> behavior at high temper-<br />
atures is suggested.<br />
Ceramic Materials. Two specimens<br />
of beryllium oxide blocks with approxi-<br />
mate dimensions 0.25 by 0.25 by 0.50<br />
in. were exposed t,o NaF-BeF2 (57-43<br />
mole %) for 100 hr (24,000 cycles) in<br />
<strong>the</strong> tilting furnace with <strong>the</strong> hot end<br />
(beryllium oxide mechanically held at<br />
hot end) at 800"CJ and <strong>the</strong> cold erld at<br />
TABLE 11.5. CORROSION OF INIONEL BY NaF-ZrF4-UF4 AT TEMPERATURES PROI $B<br />
- .I_<br />
~. .<br />
RUN NO.<br />
13 2<br />
800<br />
1000<br />
1100<br />
1200<br />
'a)Prerun analyses of fuel:<br />
("Prerun analyses of fuel:<br />
("Prerun analyses of fuel:<br />
__ .......<br />
...............<br />
WEIGHT CHANCE<br />
( mg/dm2/day 1<br />
+4<br />
+8<br />
-1<br />
+22<br />
4-9<br />
+12<br />
0<br />
+6<br />
- 13<br />
-31<br />
._ .____<br />
....<br />
...<br />
0.5 to 1<br />
0.5 to 1<br />
0.5 to 1<br />
1 to 2<br />
1 to 4<br />
1 to 4<br />
0.5 to 2<br />
0.5 to 2<br />
0.5 to 2<br />
0.5 to 1<br />
3000 ppm Fe, 980 ppm Cr, 230 ppm Ni.<br />
720 ppm Fe, >20 ppm Cr, 135 ppm Ni.<br />
340 ppm Fe, >20 ppm Cr, 580 ppm Ni.<br />
....... ~<br />
........<br />
CHEMICAL ANALYSIS (ppm) .~<br />
Fe<br />
Cr<br />
Ni<br />
170<br />
180<br />
440<br />
18 5<br />
100<br />
90<br />
95<br />
100<br />
2 00<br />
290<br />
90<br />
1860<br />
2100<br />
2700<br />
3000<br />
2600<br />
980<br />
1000<br />
1030<br />
61 0<br />
20<br />
45<br />
20<br />
20<br />
20<br />
20<br />
20<br />
20<br />
75<br />
110