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ORNL-1771 - Oak Ridge National Laboratory

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ANP QUARTERLY PROGRESS REPORT<br />

TEMPERATURE DIFFERENTIAL, 159.2OF<br />

REYNOLDS NO. AT 13OO0F, 3730<br />

REYNOLDS NO. AT 1459"F, 4540<br />

FLOW, 0.81 gprn<br />

VELOCITY, 5.29 fps<br />

MASS FLOW RATE, 0.361 Iblsec<br />

LENGTH OF HEATING SECTION, 5.13 ft<br />

LENGTH OF COOLING SECTION, 5.86 ft<br />

POWER, 17.6 kw<br />

CURRENT, 400 amp<br />

VOLTAGE, 44<br />

HEATING SECTION<br />

1<br />

<strong>ORNL</strong> - LR -DWG 3097<br />

0.02 5 -in. WALL<br />

INCONEL TUBING<br />

Fig. 3.5. Configuration and Design Conditions for lnconel Forced-Circulation Loop to Operate at a<br />

Temperature Differential of Approximately 16OOF.<br />

A summary of the design dimensions and expected<br />

operating conditions for each of the six loops is<br />

presented in Table 3.1, which also indicates the<br />

current status of each loop. Three methods of<br />

heating were studied: electr ical-res i stance, gas-<br />

fired furnace, and liquid bath. The liquid bath<br />

was discounted because it would require pres-<br />

surization of the liquid rneta1,an excessively long<br />

heat exchanger,and a large investment. A gas-<br />

fired furnace was considered, but lack of operating<br />

experience and the high heat flux necessary for<br />

the loops indicated the use of electrical heating,<br />

with which considerable experience has been ob-<br />

tained. A gas-fired furnace is being studied as a<br />

possible heat source for a large number of cor-<br />

rosion loops. Preliminary calculations of the<br />

pressure drop through the loops indicate that the<br />

40<br />

Model LFA pump8 can be used, and thus it will<br />

not be necessary to develop a pump.<br />

For purposes of preliminary design the following<br />

assumptions were made: (1) The specific resis-<br />

tivity of molten NaF-ZrF,-UF, (50-46-4 mole %)<br />

is so high that the resistance of the electrically<br />

heated lnconel tube may be taken as the parallel<br />

circuit re~istance.~ (2) Heat transfer to the<br />

fluoride mixture may be calculated by relations<br />

established for water." (3) A thermal loss equal<br />

'W. 6. McDonald et al., ANP Quar. Prog. Rep. Mar.<br />

10, 1954, <strong>ORNL</strong>-1692, p 15.<br />

n<br />

'A. L. Southern, personal communication.<br />

'OD. F. Salmon, Turbulent Heat Transfer from a<br />

Molten Fluoride Salt Mixture to NaK in a Double Tube<br />

Heat Exchanger, <strong>ORNL</strong>-1716 (to be issued).

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