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ORNL-1816 - the Molten Salt Energy Technologies Web Site

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ANP QUARTERLY PROGRESS REPORT<br />

and operation is being prepared. Modifications of<br />

this vapor trap design could be used on o<strong>the</strong>r<br />

fused salt systems in which reliable gas con-<br />

nection is important.<br />

ADlNG OF THE ARE<br />

N. V. Smith<br />

installations for <strong>the</strong><br />

loading of <strong>the</strong> ARE were completed during <strong>the</strong><br />

month of October. Transfer of <strong>the</strong> barren carrier<br />

(NaF-ZrF,, 50-50 mole %) into <strong>the</strong> ARE fill tank<br />

ompleted in approximately 43 hr<br />

t. Approximately 2750 Ib of carrier<br />

ded into <strong>the</strong> fill tank, and sufficient<br />

n hand to fill <strong>the</strong> fuel system to<br />

its operating liquid level.<br />

The enriched fuel storage tank had previously<br />

been loaded with 60 Ib of carrier material for<br />

practice injections into <strong>the</strong> reactor. Tests indi-<br />

cated that <strong>the</strong> semiautomatic enrichment system<br />

was inadequately heated, and <strong>the</strong>refore equipment<br />

for addition of portions of <strong>the</strong> fuel concentrate<br />

(Na,UF,) directly to <strong>the</strong> circulating fuel pump<br />

was designed and assembled.<br />

In order to provide adequate means for ap-<br />

proaching criticality safely, some of <strong>the</strong> original<br />

30-lb batches of concentrate were reduced to<br />

10-lb batches, and, similarly, to provide accurate<br />

measurements for calibration of <strong>the</strong> control rods<br />

after criticality, 12 small batches of approximately<br />

0.5-lb size were prepared from a 30-lb batch.<br />

The injection system consisted of a main con-<br />

centrate can (containing 30, 10, or 0.5 Ib as<br />

ed) connected to an intermediate transfer<br />

can by a resistance-heated \-in. lnconel tube.<br />

The intermediate transfer can was designed so<br />

that it could be filled to a predetermined level<br />

(approximately 5.5 Ib) when <strong>the</strong> 10- or 30-lb<br />

batches were in position to be transferred. The<br />

0.5-lb batches were transferred through a smaller<br />

intermediate can, which contained <strong>the</strong> entire small<br />

time of transfer. The intermediate can<br />

rn, connected to <strong>the</strong> fuel pump. The<br />

main transfer line to <strong>the</strong> pump was heated by<br />

calrod units, while <strong>the</strong> nozzle within <strong>the</strong> pump<br />

18<br />

was heated by resistance heating. The close<br />

tolerances of <strong>the</strong> injection nozzle resulted in an<br />

inherent tendency to short out and cause <strong>the</strong><br />

nozzle tip to be cold. This, coupled with <strong>the</strong><br />

drainage of high-melting-point material from <strong>the</strong><br />

long transfer line, always presented <strong>the</strong> possi-<br />

bility of a frozen-fluoride plug.<br />

The first 30 Ib of concentrate was injected into<br />

<strong>the</strong> fuel pump without apl;arent difficulty. After<br />

this injection, however, difficulties in <strong>the</strong> form<br />

of line plugs and venting troubles frequently<br />

occurred. After 48 hr, most of <strong>the</strong>se problems<br />

were under control, and loading of <strong>the</strong> enriched<br />

concentrate proceeded smoothly. The reactor was<br />

brought to criticality, and small injections of<br />

0.5-lb batches were made for <strong>the</strong> control rod<br />

calibrations. At <strong>the</strong> completion of <strong>the</strong> final small<br />

addition, <strong>the</strong> transfer line broke and simultane-<br />

ously plugged at <strong>the</strong> injection nozzle. Efforts to<br />

repair <strong>the</strong> damage were fruitless, and <strong>the</strong> final<br />

injection of 30 Ib of <strong>the</strong> concentrate to allow ARE<br />

operation at power was made through <strong>the</strong> sample<br />

line into <strong>the</strong> pump.<br />

ANALYSIS OF LEAK IN SODIUM SYSTEM<br />

E. E. Hoffman W. H. Cook<br />

C. F. Leitten<br />

Metal lurgy Division<br />

The sodium system of <strong>the</strong> ARE was filled<br />

initially on September 26, 1954, but <strong>the</strong> sodium<br />

had to be dumped on September 27 because of a<br />

leak at a tube bend in <strong>the</strong> sodium purification<br />

system. The section of austenitic stainless steel<br />

pipe in which <strong>the</strong> leak occurred was located just<br />

ahead of <strong>the</strong> filter traps. The system had been<br />

filled with sodium for 37 hr and had reached a<br />

maximum temperature of approximately 1150°F<br />

before <strong>the</strong> leak was detected. A portion of <strong>the</strong><br />

section removed and <strong>the</strong> location of <strong>the</strong> leak are<br />

shown in Fig. 1.6. The leak occurred where a<br />

metal <strong>the</strong>rmocouple protection tube had been at-<br />

tached to <strong>the</strong> stainless steel pipe by Heliarc<br />

welding. The attack around <strong>the</strong> weld was due to<br />

<strong>the</strong> formation of sodium oxide as <strong>the</strong> sodium<br />

leaked through <strong>the</strong> weld. The inside of <strong>the</strong> pipe<br />

at <strong>the</strong> weld may be seen in Fig. 1.7. An ex-<br />

cessive amount of penetration was obtained during<br />

<strong>the</strong> welding operation. The large weld nugget<br />

cracked during cooling after welding. A cross<br />

section of <strong>the</strong> weld crack is shown in Fig. 1.8.<br />

Examination of <strong>the</strong> pipe in this section revealed<br />

a<br />

" .<br />

.<br />

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