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Hot gas
decontamination: Hot gas decontamination is a
technology still in the pilot-scale of development that can be
used for decontamination of explosives-contaminated masonry or
metallic structures. The method involves sealing and insulating
the structures, heating with hot gas stream to 260 °C (500 °F)
for a prescribed period of time, volatilizing the explosive
contaminants, and destroying them in an afterburner. Operating
conditions are site-specific. Contaminants are completely
destroyed.
Incineration:
Incineration processes can be used to treat the following
wastestreams: explosive-contaminated soil and debris, explosives
with other organic or metals, initiating explosives, some bulk
explosives, unexploded ordnance, bulk explosive waste, and
pyrophoric waste. In addition, incineration can be applied to
sites with a mixture of media, such as sand, clay, water, and
sludge, provided the media can be fed to the incinerator and
heated for a sufficient period of time. With the approval of the
DOD Explosives Safety Board, the Army considers incineration of
materials containing less than 10% explosives by weight to be a
nonexplosive operation. Soil with less than 10% explosives by
weight has been shown by USAEC to be nonreactive; that is, not to
propagate a detonation throughout the mass of soil. (The military
explosives to which this limit applies are secondary explosives
such as TNT and RDX and their manufacturing byproducts).
The Army primarily uses three types of incineration devices:
the rotary kiln incinerator, deactivation furnace, and
contaminated waste processor.
The rotary kiln incinerator
is used primarily to treat explosives-contaminated soils. In
rotary kiln incineration, soils are fed into a primary combustion
chamber, or rotary kiln, where organic constituents are
destroyed. The temperature of gases in the primary chamber ranges
from 427 oC to 649 oC (800 oF to 1,200 oF ), and the temperature
of soils ranges from 316 oC
to 427 oC
(600 oF
to 800 oF).
Retention time in the primary chamber, which is varied by
changing the rotation speed of the kiln, is approximately 30
minutes. Off gases from the primary chamber pass into a secondary
combustion chamber, which destroys any residual organics. Gases
from the secondary combustion chamber pass into a quench tank
where they are cooled from approximately 2,000 oC
to 200 oC
(3,600 oF to 400 oF).
From the quench tank, gases pass through a Venturi scrubber and a
series of baghouse filters, which remove particulates prior to
release from the stack. The treated product of rotary kiln
incineration is ash (or treated soil), which drops from the
primary combustion chamber after organic contaminants have been
destroyed. This product is routed into a wet quench or a water
spray to remoisturize it, then transported to an interim storage
area pending receipt of chemical analytical results.
The deactivation furnace is also referred to as Army
Peculiar Equipment (APE) 1236 because it is used almost
exclusively by the Army to deactivate large quantities of small
arms cartridges, and 50-caliber machine gun ammunition, mines,
and grenades. The deactivation furnace is similar to the rotary
kiln incinerator except it is equipped with a thick-walled
primary combustion chamber capable of withstanding small
detonations. Deactivation furnaces do not have secondary
combustion chambers because they are intended not to completely
destroy the vaporized explosives but to render the munitions
unreactive. Most deactivation furnaces are equipped with air
pollution control equipment to limit lead emissions. The
operating temperature of deactivation furnaces is approximately
650 oC to 820 oC
(1,200 oF to 1,500 oF).
The contaminated waste processor handles materials,
such as surface-contaminated debris, that are lighter and less
reactive than those processed in the deactivation furnace.
Contaminated waste processors are thin-walled, stationary ovens
that heat contaminated materials to about 600 oC
(1,100 oF) for 3 to 4
hours. The purpose of this process is not to destroy contaminated
debris but to sufficiently lower contaminant levels through
volatilization to meet Army safety standards. USAEC currently is
helping to develop standardized time and temperature processing
requirements to meet these safety standards.
Open Burn/Open Detonation:
Open burn (OB) and open detonation (OD) operations are conducted
to destroy unserviceable, unstable, or unusable munitions and
explosive materials. In OB operations, explosives or munitions
are destroyed by self-sustained combustion, which is ignited by
an external source, such as flame, heat, or a detonation wave. In
OD operations, detonable explosives and munitions are destroyed
by a detonation initiated by a disposal charge. OB/OD operations
require regulatory permits. These permits must be obtained from
the appropriate regulatory agency on a case-by-case basis.
OB/OD operations can destroy many types of explosives,
pyrotechnics, and propellants. OB areas must be able to withstand
accidental detonation of any or all explosives being destroyed,
unless the characteristic of the materials involved is such that
orderly burning without detonation can be ensured. Personnel with
this type of knowledge must be consulted before any attempt is
made at OB disposal, especially if primary explosives are present
in any quantity.
OB and OD can be initiated either by electric or burning
ignition systems. In general, electric systems are preferable
because they provide better control over the timing of the
initiation. In an electric system, electric current heats a
bridge wire, which ignites a primary explosive or pyrotechnic,
which in turn ignite or detonate the material slated to be burned
or detonated. If necessary, safety fuses, which consist of
propellants wrapped in plastic weather stripping, are used to
initiate the burn or detonation.
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