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ORNL-4191 - the Molten Salt Energy Technologies Web Site

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BeF, in 2LiF 13eF,, this partial pressure was<br />

found to be surprisingly low, that is, 0.03 mm at<br />

700'K to 21 mm at 1000'K. Flir<strong>the</strong>rmore, pre-<br />

liminary direct measurements now in progress con-<br />

firm <strong>the</strong> low range of <strong>the</strong>se partial pressures. This<br />

suggested that an overpressure of SiF , might pre-<br />

vent, or at least reduce, <strong>the</strong> attack of <strong>the</strong> silica<br />

container and prevent <strong>the</strong> precipitation of BeO.<br />

The compatibility of SiO, with <strong>the</strong>se LiF-BeF ,<br />

melts is primarily associated with <strong>the</strong> relative<br />

stability of BeF, compared with that of BeO; <strong>the</strong><br />

standard free energies of formation at 1000°K are<br />

-206 and -120 kcal/mole respectively. Since<br />

many o<strong>the</strong>r metallic fluorides show even greater<br />

stability compared with <strong>the</strong>ir corresponding oxides,<br />

it seems that Si0, should not be ruled out as a<br />

container material for molten fluorides without<br />

first estimating <strong>the</strong> equilibrium position of such<br />

reactions as<br />

X<br />

--SiQ,(s) i MFx(s or I ) + MOx,,(s)<br />

4<br />

X<br />

+ --SiF,(g) , (4)<br />

4<br />

which involve <strong>the</strong> pure metal fluoride and metal<br />

oxide, and<br />

The latter reaction is <strong>the</strong> one of most interest,<br />

since it gives <strong>the</strong> level of oxide contamination<br />

of <strong>the</strong> fluoride melt. Its equilibrium position may<br />

be judged if activity coefficients or solubilities<br />

can be assigned to MFx and MOxiz in <strong>the</strong> melt<br />

under consideration. In <strong>the</strong> present case <strong>the</strong> activity<br />

of BeF, in 2LiF. BeF, (",0.03) and <strong>the</strong><br />

solubility of He0 (-0.01 mole of 0'- per kg of<br />

salt at 600'C) have been measured. From <strong>the</strong>se<br />

and <strong>the</strong> available <strong>the</strong>rmochemical data <strong>the</strong> following<br />

equilibrium quotient may be estimated for <strong>the</strong><br />

above reaction [Eq. (5)l in 2LiF. BeF, at 600°C:<br />

7C. F. Baes, Jr., "The Chemistry and Thermodynamics<br />

of <strong>Molten</strong> <strong>Salt</strong> Reactor Fluoride Solutions," SM-66/60<br />

in Thermodynamics, vol. 1, IAEA, Vienna.<br />

138<br />

From this, it can in turn be estimated that in <strong>the</strong><br />

presence of 1 atm of SiF, <strong>the</strong> oxide ion concentration<br />

at equilibrium with SiO, should be only<br />

6 x lo-, mole/kg.<br />

Ano<strong>the</strong>r factor to be considered when using silica<br />

is <strong>the</strong> possible formation of silicates; for<br />

example,<br />

2MF,(s or 2) i 2SiO,(s)<br />

In <strong>the</strong> present case, for example, Be,SiO, (phen-<br />

acite) should be formed as <strong>the</strong> stable reaction<br />

product ra<strong>the</strong>r than ReQ at low SiF, partial pres--<br />

suies; however, phenacite is not very stable rcl-<br />

ative to 2He0 -I SiO, and should not alter <strong>the</strong><br />

above conclusions about <strong>the</strong> compatibility of sil-<br />

ica with LiF-BeF, melts. In o<strong>the</strong>r fluoride sys-<br />

tems, <strong>the</strong> formation of metallic silicates may be<br />

<strong>the</strong> controlling factor.<br />

The solubility of SiF, in <strong>the</strong> molten fluoride<br />

must be considered because possible reactions<br />

such as<br />

could produce high solubilities which not only<br />

would alter <strong>the</strong> salt phase, but also would cause<br />

<strong>the</strong> reaction with SiO, to proceed far<strong>the</strong>r than<br />

o<strong>the</strong>rwise expected. Accordingly, <strong>the</strong> solubility<br />

of SiF , in 2LiF . BeF was estimated by means<br />

of transpiration measurements. The prepurifjed<br />

salt was saturated with SiF, by bubbling a mix-<br />

ture of 0 1 atiii of SiF, in He through <strong>the</strong> salt<br />

until <strong>the</strong> effluent and influent compositions were<br />

<strong>the</strong> same. The dissolved gas was <strong>the</strong>n stripped<br />

with helium and trapped in an aqueous NaOH bub-<br />

bler, <strong>the</strong> amount of SiF , being equivalent to <strong>the</strong><br />

amount of NaOH consumed by its hydrolysis:<br />

SiF,(g) i- 40H- + 4F- + 2H,0 I SiO,(s) . (9)<br />

The solubility was calculated by means of<br />

in which

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