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7.0 Application Examples; Feed Preparation Example
The equation as used in this case has already been multiplied by the factor of two
necessary to obtain a bounding value. It is noted that the absolute density of
plutonium oxide (11.5 g/cm3) was not used. The equation requires the use of bulk
powder density, which must take void volume into account. The value of 2.5 g/cm3
used is representative of heavy metal oxides such as plutonium oxide.
The value of ARF obtained from this equation is not directly related to the bounding
RF of 0.3 assigned. While it may be adequate to assume the 0.3 value for spill
distances greater than 3 m, it is not for distances significantly less than 3 m as the
small fall distance minimizes the time for particulate interaction and agglomeration.
The equation provided in subsection 4.4.3.1.2 for estimating particle size is:
AMMD = 12.1 - 3.29(
) + 7540(ARF)
(7-3, 4-6)
BP
where:
AMMD
= aerodynamic equivalent mass median diameter
= 5 m,
= bulk powder density = 2.5 g/cm3, and
BP
ARF
= airborne release fraction = 1.5E-4.
An AMMD of 5 m would indicate an RF significantly higher than 0.3, producing a
combined ARF x RF of ~ 1E-4. This is a factor of 6 less than the combined
ARF x RF (6E-4) assessed for fall distances less than 3 m, and approximately the
same as the median ARF x RF (1.5E-4) estimate provided in the handbook for
perspective on conservatism. For the types of estimates being made, there is not a
major difference between the two values. Either estimate could be defended, but for
the sake of conservatism and consistency, the bounding value is used.
B. Ignition of Plutonium Metal Fines. If plutonium metal fines are present in an
oxide container opened in an oxygen environment, it is not uncommon to see brief
sparking after opening. This is generally not a major concern due to the limited
amount of fines. Even if a given small piece of metal sustains smoldering oxidation,
the overall fire hazard is minimal. The metal is not in close proximity to a significant
amount of combustible material with which to interact; it will generally cease
combustion due to heat transfer losses through metal surfaces, and the combustion can
easily be extinguished by the operator simply by closing the container.
The hazard identification states that 100 g of metal fines is the maximum amount of
metal contamination anticipated in impure oxide received for processing. The
absolute limit is 2000 g if an entire feed can contains nothing but metal fines, but the
maximum anticipated DR is 0.05. The DR for metal fines present is never
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