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ORNL-2106 - the Molten Salt Energy Technologies Web Site

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ANP PROJECT PROGRESS REPORT<br />

TABLE 2.3.1. SUMMARY OF VAPOR PRESSURES FOR THE SYSTEM KF-ZrF, c,<br />

Composition Heat of<br />

Constants<br />

Vaporization<br />

Experimental Temperature (mole X) of ZrF4, &I,,<br />

Range (OC) A €3<br />

ZrF4 KF<br />

(kcal/mole)<br />

in <strong>the</strong> relation<br />

750-900 65.9 34.1 9.754 8,813 40.4<br />

750-900 59.6 40.4 9.142 8,321 38.1<br />

775-900 55.0 45.0 8.403 7,778 35.6<br />

825-950 49.9 50.1 7.722 7,363 33.7<br />

875-950 47.3 52.4 7.679 7,467 34.2<br />

950- 1000 45.3 54.7 7.649 7,721 35.3<br />

975-1 100 40.4 59.6 7.612 8,465 38.8<br />

1 125-1 300 34.9 65.1 7.387 9,020 41.3<br />

B<br />

log P (mm Hg) = A - -<br />

T '<br />

where T is in OK. These constants are obtained<br />

by treating <strong>the</strong> data by <strong>the</strong> method of least<br />

squares. The heat of vaporization, AH,, of ZrF,<br />

is obtained by multiplying <strong>the</strong> constant B by<br />

2.303 (OR) or 4.576. The values listed in Table<br />

2.3.1 are considered to be more reliable than<br />

those previously published., Apparently <strong>the</strong>re<br />

was some free ZrF, present in some of <strong>the</strong> earlier<br />

experiments, and for <strong>the</strong> compositions containing<br />

65.9 to 49.9 mole % ZrF, a reanalysis by least<br />

squares gave <strong>the</strong> new constants. A plot of <strong>the</strong><br />

data from which <strong>the</strong> equation for each mixture was<br />

obtained is shown in Fig. 2.3.1.<br />

A very odd phenomenon is observed when <strong>the</strong><br />

apparent heat of vaporization, AH,, is plotted<br />

against composition (Fig. 2.3.2). A sharp minimum<br />

occurs at 50 mole % ZrF, and <strong>the</strong> heat of vaporization<br />

increases linearly with composition in both<br />

directions from <strong>the</strong> minimum. The change below<br />

50 mole % ZrF, is in <strong>the</strong> expected direction, since<br />

ZrF, becomes more tightly complexed by fluoride<br />

ions. The change above 50 mole % was not<br />

expected; qualitatively it can be explained by<br />

assuming that ZrF, exhibits positive deviations<br />

from Raoult's law when dissolved in KZrF,.<br />

00<br />

(This version of Raoult's law calls for a twoparticle"<br />

depression at <strong>the</strong> ZrF, end of <strong>the</strong><br />

composition range and for zero pressure at <strong>the</strong><br />

KZrF, end.) In practice, <strong>the</strong> vapor pressure of<br />

supercooled liquid ZrF, is not sufficiently well<br />

112<br />

known for a numerically reliable Raoult law to<br />

be established for ZrF, systems at 600 to 800°C.<br />

The System RbF-ZrF,<br />

The vapor pressures of various mixtures in <strong>the</strong><br />

system RbF-ZrF, were determined in <strong>the</strong> same<br />

manner as in <strong>the</strong> KF-ZrF, system. Reasonably<br />

pure RbF was obtained by selecting clear crystals<br />

from a slowly cooled melt. Analyses showed that<br />

<strong>the</strong> o<strong>the</strong>r alkali metal ions were present in <strong>the</strong><br />

following weight percentages: Li, 0.023; Na,<br />

0.005; K, 0.16; Cs, 0.24.<br />

The data for various mixtures are compiled in<br />

Table 2.3.2 and shown graphically in Fig. 2.3.3.<br />

The constants A and B are from <strong>the</strong> relation<br />

B<br />

log P (mm Hg) = A - -<br />

T '<br />

where T is in OK.<br />

As in <strong>the</strong> case of <strong>the</strong> KF-ZrF, system, <strong>the</strong> heat<br />

of vaporization goes through a minimum at 50 c<br />

mole % ZrF, (Fig. 2.3.4). The linearity with mole<br />

fraction is also similar to that of <strong>the</strong> KF-ZrF,<br />

system. Thus <strong>the</strong> effect seems to be a real one<br />

in spite of its unnatural appearance.<br />

A comparison of <strong>the</strong> effects of <strong>the</strong> various alkali<br />

fluorides is given in Fig. 2.3.5, in which pressure<br />

is plotted as a function of composition at 912OC,<br />

<strong>the</strong> melting point of pure ZrF,. Moore8 has<br />

siudied two compositions for <strong>the</strong> system LiF-ZrF,,<br />

-<br />

and Sense et al.' of Battelle Memorial Institute<br />

and Moore"' have studied <strong>the</strong> NaF-ZrF, system.<br />

8R. E. Moore, ANP Quat. Ptog. Rep. June 10, 19.55,<br />

<strong>ORNL</strong>-1896, P 81.<br />

LJ<br />

I

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