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DOE-HDBK-3010-94
Appendix B; Plutonium Recovery Facility
transfer to the glovebox itself, and is equipped with a hopper that physically prevents
operators from reaching into the impaction area. The machine also is interlocked to shut off
if the gloveport covers for this area are not in place during operation.
The impactor provides output material less than 1 inch in particle size. This material is then
weighed and batched in the same manner as oxide. Only one set of impacted residue is
allowed unbatched at a time to prevent inadvertent mixing of already assayed material, and
the impactor unit is monitored continuously for holdup.
Once material has been placed in one of the spring-loaded batching cans, it can temporarily
be placed in a shielded metal storage rack. The storage compartment can hold up to six
batching cans at a time. When material is needed in the appropriate dissolving line, the
chainveyor access door is opened and the batch can is placed in one of the carriers on the
chainveyor system. The carrier is then sealed and the operator directs the material to either
the oxide or the residue dissolution line.
2.2.2.2 D issolvin g L in e
The dissolving line consists of three physically separate gloveboxes installed as a single
mounted unit. The three gloveboxes are for oxide, residue, and metal dissolution
respectively. Feed to the oxide and residue gloveboxes comes from the feed preparation
chainveyor. Feed to the metal dissolution glovebox is provided by a hood and airlock
arrangement identical to that on the feed preparation glovebox. Feed material for the metal
dissolution line comes directly from the H-12 Plutonium Vault Facility and consists of
recycle material ready for processing upon receipt.
2.2.2.2.1
O xid e D issolu tion
A simple representation of the oxide dissolution process is presented as Figure B.6.
Plutonium oxide is dissolved in a concentrated nitric acid solution with fluoride
catalyst (from potassium fluoride) at near boiling temperatures. Aluminum nitrate
nonahydrate is added once dissolution is complete to minimize corrosion and break up
any plutonium and fluoride complexes formed. The dissolver solution is transferred
via air eductor vacuum through a cartridge filter to the vacuum run tank. The liquid
is then transferred to the accountability tank through another cartridge filter by means
of a liquid-to-liquid mixing eductor. From the accountability tank, liquid is
transferred via a small gear pump to tank farm vessel #1 or #2.
The dissolver is a 30-liter slab vessel with a mechanical agitator. Numerous
connection lines to the dissolver include a purge/flush line, a sample line, chemical
Page B-27


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