ORNL-1771 - Oak Ridge National Laboratory
ORNL-1771 - Oak Ridge National Laboratory
ORNL-1771 - Oak Ridge National Laboratory
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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