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ORNL-1771 - Oak Ridge National Laboratory

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ANP QUARTERLY PROGRESS REPORT<br />

Burner<br />

TABLE 3.2. EXPLORATORY TESTS OF GAS BURNERS<br />

<strong>ORNL</strong> 2.1 (max) 170<br />

Furnace<br />

Gas Rate Rate of Heat Temperature*<br />

(cfm) Release* (Btu/sec.ft 1<br />

(OF)<br />

Fisher, laboratory type 3.5 160<br />

Remarks<br />

2000 Flame did not fill<br />

combustion space on<br />

which rate was based<br />

Rate based on esti-<br />

mated flame dimensions<br />

<strong>National</strong> N-4 1.2 20 Maximum attainable<br />

Two-in. pipe with let 1.3 20 2900<br />

*These values are the highest that were attained in the test but do not necessarily represent the maximum volues<br />

attainable, except where indicated.<br />

on the cavitation phenomenon in forced-circulation<br />

high-temperature sodium systems, a preliminary<br />

study was initiated,<br />

Tests were run on the ARE hot pump test facility<br />

in which pressures at the venturi throat could be<br />

varied by varying the pressure of the blanketing<br />

gas. Thus it was possible to vary the pressures<br />

without changing the pump speed, the throttle<br />

valve setting, or the temperature. Data were taken<br />

during eight runs at temperatures in the range<br />

1200 to 1500’F. Measurements were made of pump<br />

discharge pressure, venturi throat pressure, and<br />

pump suction pressure as the pump suction pres-<br />

sure was varied. Cavitation was found to begin<br />

when the venturi throat pressure ceased to decrease<br />

uniformly with decreasing pump suction pressure.<br />

Also, as cavitation began, the loop pressure drop<br />

increased and the flow rate decreased. Observation<br />

of fluid flow noise revealed a correlation of noise<br />

intensity with pressure data.<br />

The pressure at which cavitation occurred cannot<br />

be exactly ascertained, since the pressure at the<br />

middle of the throat of the venturi is obviously<br />

not the lowest pressure in the venturi. In water<br />

cavitation, bubbles form at the start of the flow<br />

expansion, and, in the particular venturi used, the<br />

rather sharp radius at the transition from the throat<br />

to the diffusion cone probably caused flow sepa-<br />

ration. The minimum pressures observed at the<br />

throat were within 1 psi of the vapor pressure of<br />

sodium.<br />

42<br />

Instrumentation for measurement of subatmos-<br />

pheric pressures was required for these high-<br />

temperature (up to 1500°F) sodium-cavitation<br />

studies. A Moore nul I-balance bel lows-type pres-<br />

sure transmitter and a Moore Model 60-N “nullmaticf’<br />

pilot valve modified to vent the pilot volve to a<br />

vacuum source proved to be satisfactory for this<br />

application. When the venting atmosphere or sink<br />

pressure is reduced, the unit is capable of meas-<br />

uring correspondingly lower process pressures.<br />

Pressure measurements were made over the range<br />

of 20 to 1.6 psia, with the sodium-filled transmitter<br />

maintained at about 65OOF. The zero shift of the<br />

pressure transmitter ranged from 4.3 to -0.2 in.<br />

tig over the range.<br />

A second check of the zero shift was made as<br />

the transmitter temperature was varied from 800 to<br />

470’F with a constant system pressure of approxi-<br />

mately 16.2 psiu. The zero shift then observed was<br />

+0.1 to -0.2 in. tig. In general, the performance<br />

of this pressure-measuring device was quite sotis-<br />

factory; a more highly refined application of this<br />

device might lead PO even smaller zero shift. A<br />

report covering this modification is being prepared.<br />

EXPANSION AND IMPROVEMENT Of THERMAL-<br />

CONVECTION LOOP TESTING FAClLlTlES<br />

E. M. Lees<br />

Aircraft Reactor Engineering Division<br />

The number of power panels installed for sup-<br />

plying thermal-convection loops has been expanded

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