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ORNL-1771 - Oak Ridge National Laboratory

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-<br />

PERIOD ENDING SEPTEMBER 10, 1954<br />

TASLE 3.1. PRINCIPAL FEATURES AND STATUS OF FORCED-C1FtCULAflON CORROSION LOOPS<br />

__._......_..i__-...... ~<br />

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

......... ...~~~.-...-..I___ -I____.. ____ ._..--......<br />

Loop Number<br />

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

1 2 3 4 5 6<br />

Reynolds number at 1500'F 10,000 1 0,000 10,000 800 3000<br />

Temperature differential, OF 100 2 00 300 200 2 00<br />

Power input, kw 27.7 54.2 80,O 6.8 25.5<br />

Heating section length, ft* 8.08 8.08 8.08 6 22.3<br />

Cooling section length, ft* 15.64 15.64 15.64 1.6 6<br />

Heat exchanger length, ft** 18.75 18.75 18.75 None Nons<br />

Pressure drop, psi 35.12 36-54 47.5 0.06 0.57<br />

Status Detail Detail Construction Detail Pre I i mi nary<br />

design<br />

complete<br />

design<br />

complete<br />

and assembly<br />

80% complete<br />

design<br />

90%<br />

complete<br />

design<br />

complete;<br />

detail design<br />

20%<br />

comp lete<br />

. ..<br />

~ ~<br />

"OS-in.-OD, 0.020- in.-wal I tubing.<br />

**loo-in.-OD, 0.049-in,-wall tubing used for outer tube of concentric-tube heat exchanger.<br />

to 10% of the total heat transfer exists at the<br />

heater section and at the heat exchanger.<br />

Diosimi lor-Metal Loops<br />

L. A. Mann<br />

Aircraft Reactor Engineering Division<br />

A loop for testing combinations of structural<br />

metals in contact with high-velocity turbulent<br />

liquid metals under high temperature differentials<br />

is being developed, If combinations of materials<br />

are found that ore satisfactory for use in liquid<br />

metal systems, greater flexibility and ease of<br />

construction may be attained. An optimized design,<br />

patterned after that used for beryllium-lnconel-<br />

sodium mass transfer tests (cf. Sec. 2, "Reflector-<br />

Moderated Reactor"), has been developed and is<br />

to be used first for testing combinations of lnconel<br />

and type 316 stainless steel in sodium.<br />

GAS- F U R N AC E HE A +-SOU RC E DE V EL 0 P M E N T<br />

L. A. Mann<br />

Aircraft Reactor Engineering Division<br />

L. F. Roy"<br />

University OF Mississippi<br />

Several exploratory tests were made OQ cam-<br />

mercial and QRNL-designed-and-fabricated burners<br />

for use with the gas-furnace heat source described<br />

previously. l 2 The heat release intensity desired<br />

15,000<br />

200<br />

86.9<br />

8.08<br />

15.44<br />

18.75<br />

1 15.5<br />

Construct ion<br />

20% com-<br />

plete<br />

is on the order of 3000 Btu/ft3.sec, which is of the<br />

same order as that attained in iet aircraft burners.<br />

The maximum rate of heat release obtained in<br />

the tests, 170 Btu/ft3, was obtained with the<br />

burner designed by A. P. Fraas. The results of<br />

these exploratory tests are presented in Table 3.2.<br />

Although the rate of heat release contemplated in<br />

the original design (about 3000 Btu/ft3.sec) was<br />

not approached in these tests, it appears that<br />

rates higher than 170 Btu/ft3.sec can be attained<br />

by securing more rapid mixing of air and gas,<br />

preheating the combustion-air, and providing a<br />

positive pressure in the combustion chamber.<br />

Additional tests are to be made.<br />

STUDY OF THE CAVITATION PHENOMENON<br />

W. G. Cobb A. G. Grindell<br />

J. M. TrummeI<br />

Aircraft Reactor Engineering Division<br />

G. F. Wislicenus, Consultant<br />

One of the problems associated with operating<br />

liquid metal systems at elevated temperatures,<br />

high flow rates, high pump speeds, and minimum<br />

container weight is that of local boiling or cavi-<br />

tation. Because there is little information available<br />

'Summea ~csearch Participant.<br />

"A. P. Fi-~iis, R. W. Bussard, R. E. McPherson, ANF'<br />

Qutar. Frog:, Krp. jzine 10, 1954, <strong>ORNL</strong>-1729, p 23.<br />

41

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