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ORNL-4191 - the Molten Salt Energy Technologies Web Site

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Part 6. <strong>Molten</strong>-<strong>Salt</strong> Processing and Preparation<br />

M. E. Whatley<br />

We have continued development work on <strong>the</strong> more<br />

critical parts of <strong>the</strong> fuel processing system for an<br />

MSBR. The basic concept of an on-site plant which<br />

will continuously process 14 ft3 of fuel salt per day<br />

through a fluorination operation to recover <strong>the</strong> ura-<br />

nium, a distillation operation to separate <strong>the</strong> carrier<br />

salt from <strong>the</strong> lees-volatile fission products, and a<br />

recombination of <strong>the</strong> purified carrier salt and uranium<br />

remains unchanged. The area of work which has re-<br />

ceived most attention during this period is <strong>the</strong> dis-<br />

tillation operation. Relative volatility values have<br />

been more accurately determined and extended to<br />

additional fission product poisons. The technique<br />

of using a transpirational method for relative vol-<br />

atility measurement is being exploited. We have<br />

fabricated <strong>the</strong> experimental still which will be used<br />

at <strong>the</strong> MSRE to demonstrate distillation of radioactive<br />

salt, and it will be tested soon. The alternative<br />

process, removal of rare-earth fission products by<br />

reductive extraction, still appears promising; <strong>the</strong>re-<br />

fore, this work is continuing. The problem of heat<br />

generation in <strong>the</strong> various components of <strong>the</strong> process-<br />

ing plant is being elucidated by a new computer code<br />

which will provide concentrat.ions of individual fis-<br />

sion products with adequate accuracy for this purpose.<br />

We tiow plan to recover <strong>the</strong> uranium from <strong>the</strong> MSRE<br />

in early 1968, with a cooling t.ime of only 35 days;<br />

for this procedure some modification of <strong>the</strong> process-<br />

ing cell will be necessary. The new loading of <strong>the</strong><br />

MSRE in 1968 will use 233U. Plans for <strong>the</strong> prepara-<br />

tion of this fuel are reported here.<br />

20. Vapor-Liquid Equilibrium Data in <strong>Molten</strong>-<strong>Salt</strong> Mixtures<br />

J. K. Hightower L. E. McNeese<br />

Relative volatilities of several rare-earth trifluorides having <strong>the</strong> desired composition was melted in a<br />

arid alkaline-earth fluorides with respect to LiF have graphite crucible. The mixture was <strong>the</strong>n cooled to<br />

been measured in an equilibrium stilt at 1000°C. The room temperature, and <strong>the</strong> resulting salt ingot was<br />

measured relative volatilities are in close agreement loaded into <strong>the</strong> 1 '$-in.-diarn section of <strong>the</strong> still.<br />

with those predicted by Kaoult's law and are low The still was welded shut, <strong>the</strong> condenser section<br />

enough that a simple distillation system will work was insulated, and <strong>the</strong> still was suspended in <strong>the</strong><br />

well for removing rare-earth fission products from <strong>the</strong> furnace. Air was purged from <strong>the</strong> system by re-<br />

MSRE fuel stream.<br />

peatedly evacuating <strong>the</strong> system and filling to at-<br />

The equilibrium still used for <strong>the</strong>se measurerrients mospheric pressure with argon, and <strong>the</strong> pressure<br />

is shown in Fig. 20.1. The still consists of a 1%- was set at <strong>the</strong> desired level. The furnace temperain.-diam<br />

still pot, a 1-in.-diam conderiser, and a trap ture was raised to 1000°C and <strong>the</strong> condenser ternthrough<br />

which condensate flows prior to its return to perature set at <strong>the</strong> desired value. During runs with<br />

<strong>the</strong> still pot. For each experiment, a salt charge a given component dissolved in LiF, <strong>the</strong> operating<br />

239

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