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ANP PROJECT QUARTERLY PROGRESS REPORT<br />

has been developed. A thin-walled<br />

metal tube with a small diameter is<br />

immersed in <strong>the</strong> liquid being studied,<br />

and <strong>the</strong> tube is suddenly heated by a<br />

direct current of electricity. The<br />

transient temperature rise of <strong>the</strong><br />

tube is a function of <strong>the</strong> heat capacity<br />

of <strong>the</strong> tube and <strong>the</strong> <strong>the</strong>rmal conduc-<br />

tivity, heat capacity, and density of<br />

<strong>the</strong> liquid. The early part of <strong>the</strong><br />

temperature-time function is completely<br />

controlled by <strong>the</strong> conduction mechanism.<br />

Analyses of <strong>the</strong> solutions of <strong>the</strong><br />

transient conduction equations per-<br />

taining to <strong>the</strong> system described(')<br />

show that 1 i quid <strong>the</strong>rm a 1 conduct ivi ti e s<br />

may he determined from <strong>the</strong> experi-<br />

mental temperature- time measuremenLs.<br />

This transient apparatus has been used<br />

to check <strong>the</strong> <strong>the</strong>rmal conductivity of<br />

water and glycerine at. room tempera-<br />

ture; <strong>the</strong> results agree to within<br />

+lo% of <strong>the</strong> values reported in <strong>the</strong> lit-<br />

erature.<br />

In addition to <strong>the</strong> continued study<br />

of fluoride salt mixtures, it is<br />

planned to measure<br />

ductivity of molten<br />

by oneor more of <strong>the</strong><br />

above.<br />

HEAT CAPACITY<br />

<strong>the</strong> <strong>the</strong>rmal con-<br />

sodium hydroxide<br />

met hods d i s cus sed<br />

OF LIQUIDS<br />

W. D. Powers<br />

G. C. Blalock<br />

Re act 0 r Expe rime n t a1 Engineering<br />

Division<br />

The enthalpy and <strong>the</strong> heat capacity<br />

of <strong>the</strong> fuel mixture NaF-KF-ZrF, -UF,<br />

(4.8-50.1-41.3-3.8 mole %) have been<br />

determined by Bunsen ice calorimeters<br />

for <strong>the</strong> temperature range of 540 to<br />

900°C and are given by <strong>the</strong> equations:<br />

H, (liquid) - HOoC (solid)<br />

= -15 + 0.28T ,<br />

c = 0.28 f 0.015 ,<br />

P<br />

where H is in cal/g, 7' in OC, and cP<br />

in cal/g-OC. The fuel mixture<br />

NaF-ZrF4-UF, (50-46-4 mole %) and <strong>the</strong><br />

(2)W. 8. Harrison, Transient Methods for<br />

Determining Thermal Conductivrty of Liquids,<br />

OWL CF-52-11-113 (Nor. 1, 1952).<br />

176<br />

eutectic mixture of NaOH and LiOII are<br />

currently being studied.<br />

VISCOSITPES OF FLUORIDE MIXTURES<br />

measurements with <strong>the</strong>! Brook field<br />

Viscometer (R. F. Redmond, T. N. Jones,<br />

Reactor Experimental Engineering<br />

Division). The viscosities of <strong>the</strong><br />

fluoride salt mixtures NaF-ZrF4 (SO-SO<br />

mole %) and NaF-ZrF,-UF, (50-25-25<br />

mole %) have been measured with a<br />

Brookfield viscometer contained in an<br />

inert atmosphere. These results are<br />

plotted in Fig. 13.2, toge<strong>the</strong>r with<br />

<strong>the</strong> viscosities of several o<strong>the</strong>r<br />

f 1 uori de mixtures. The zirconiumbearing<br />

salts have much higher viscosities<br />

than NaF-KF-LiF (11.5-42.0-<br />

46.5 mole %) and NaF-KF-LiF-UF,<br />

(10.9-43.5-4'4.5-1, 1 mole %); <strong>the</strong><br />

beryllium-bearing fluoride mixture<br />

NaF-BeF, (57.0-43.0 mole %) is also<br />

characterized by higher viscosities.<br />

In general, it appears that an increase<br />

in uranj urn content yields an increase<br />

in <strong>the</strong> viscosity.<br />

Capillary Viscometer (F. A. Knox,<br />

N. V. Smith, F. Kertesz, Materials<br />

Chemi stry Di vi sion) . The c api 11 ary<br />

viscometer previously<br />

has been used to study fused fluorides<br />

over <strong>the</strong> temperature range of 600 to<br />

800°C. All <strong>the</strong> materials studied in<br />

this apparatus were purified by <strong>the</strong><br />

hydrogen at i o n - hyd r o f 1 u o r i n at i on<br />

procedure. The apparatus in its present<br />

form does not sufficiently protect <strong>the</strong><br />

mixtures from exposure to air, and<br />

modifications are being made to <strong>the</strong><br />

equipment to improve <strong>the</strong> quality of<br />

<strong>the</strong> inert atmosphere maintained over<br />

<strong>the</strong> melt.<br />

Bloom, Harrap, and Heymann(')<br />

determined values for <strong>the</strong> viscosity<br />

of various chloride<br />

__ mixtures by using<br />

(3)J. M. Ciaar, F. A. Knox, F. Kertesz, R. F.<br />

Redaond, and T. N. Jones, ANP Quor. Prog. Rep.<br />

June 10, 1952, ORNL-1294, p. 146.<br />

(4)F. A. Knox, N. V. Smith, and F. Kertesz.<br />

ANP Quar. Prog. Rep. Sept. 10, 1 952, ORNL-1375,<br />

p. 145.<br />

("H. Bloom, B. S. Harrap, S. E. Neymann,<br />

Proc. Roy. SOC. (London) 194.4, 237 (1948).

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