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ORNL-1771 - Oak Ridge National Laboratory

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8. HEAT TRANSFER AND PHYSICAL PROPERTIES<br />

The enthalpies and heat capacities of NaF-ZrF,-<br />

UF, (65-15-20 mole %) were determined; the heat<br />

capacity in the solid state over the temperature<br />

range 90 to 614°C WQS found to be 0.17 cal/g."C,<br />

and the heat capacity in the liquid state over the<br />

temperature range 653 to 924°C was found to be<br />

0.20 cal/g."C. The enthalpies and heat capacities<br />

of LiF-NoF-UF4 (57.6-38.4-4.0 mole %) were also<br />

obtained; the heat capacity in the solid state over<br />

the temperature range 97 to 594°C was found to<br />

be 0.23 cal/g.OC, and in the liquid state over the<br />

range 655 to 916°C it was found to be 0.53<br />

cal/geoC. The thermal conductivities of three<br />

fluoride mixtures in the solid state at normal<br />

temperatures were determined. The conductivity<br />

of NaF-KF-UF4 (46.5-26.0-27.5 mole %) was 0.7<br />

Btu/hrsft2 ("F/ft), that for KF-Li F-NaF-UF4 (43.5-<br />

44.5-10.9-1.1 mole %) was 2.0 Btu/hr.ft* ("F/ft),<br />

and that for LiF-KF-UF, (48.0-48.0-4.0 mole %)<br />

was 1.4 Btu/hnr.ft2 (OF/ft). A new electrical con-<br />

ductivity device has been constructed and has<br />

been successfully checked with molten salts of<br />

known conductivity.<br />

Additional forced-convection heat transfer meas-<br />

urements of molten NaF-KF-LiF (1 1.5-42.0-46.5<br />

mole %) have been made. Measured thermal con-<br />

ductivities and thicknesses of insoluble deposits<br />

on the inner walls of lnconel heat transfer tubes<br />

made it possible to calculate the thermal re-<br />

sistance of the deposit. The calculated value was<br />

in good agreement with values previously deduced<br />

from the heat transfer measurements, A device<br />

for studying the rates of growth of tube-wall de-<br />

posits has been successfully tested with a simple<br />

heat transfer salt. A hydrodynamic flow system<br />

to be used for studying the reflector-moderated<br />

reactor flow structure has been tested. A mathe-<br />

matical study of the temperature structure in con-<br />

verging and diverging channel systems that duct<br />

fluids with volume heat sources has been made.<br />

A study of wall-cooling requirements in circu-<br />

lating-fuel reactors was made.<br />

'W. D. Powers and G. C. Blalock, Meut Capucztzps<br />

o/ Conipositims No. 39 and 101. <strong>ORNL</strong> CF-54-8-135<br />

(to be issued).<br />

H. F. Poppendiek<br />

Reactor Experimental Engineering Div i si on<br />

PERIOD ENDING SEPTEMBER 70, 1954<br />

PHYSICAL PROPERTIES MEASUREMENTS<br />

Heat Capacity<br />

W. D. Powers<br />

Reactor Experimental Engineering Division<br />

The enthalpies and heat capacities of two fluoride<br />

mixtures have been determined with Bunsen<br />

i ce ca I or i met ers : '<br />

NaF-ZrF4-UF, (65-15-20 mole 70)<br />

Solid (90 to 614°C)<br />

[IT - fiOoC = -3 + 0.17T<br />

Cp = 0.17 5 0.01<br />

Liquid (653 to 924°C)<br />

HT - HogC = 22 + 0.20T<br />

cp = 0.20 5 0.02<br />

LiF-NaF-UF, (57.6-38.4-4.0 mole %)<br />

Solid (97 to 594°C)<br />

HT - Hoot -= G.22(7)T 4 0.0G017T2<br />

Liquid (655 to 976°C)<br />

Cp = 0.22(7) + 0.000331'<br />

Hr - HOoC = -68 + 0.53T<br />

Cp - 0.53 -t 0.04<br />

In these expressions H is the enthalpy in cal/g,<br />

C is the heat capacity in cal/g."C, and T is the<br />

P<br />

temperature in "C. The experimental enthalpy data<br />

for LiF-NaF-UF4 (57.6-38.4-4.0 mole %) are plotted<br />

in Fig. 8.1.<br />

Automatic Simplytrol units have been added to<br />

the calorimeter systems to more accurately control<br />

the furnace temperatures. This modification has<br />

increased the precision of the experimental data.<br />

Currently, enthalpies of a fluoride mixture are<br />

being measured with the copper block calorimeter.<br />

Density and Viscosity<br />

S. I. Cohen<br />

Reactor Experimental Engineering Division<br />

Prel iminary density measurements were made on<br />

rubidium metal, and the density was found to be<br />

represented by the equation<br />

p(g/cm3) = 1.52 - 0.00054 (T - 39°C) ,<br />

127

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