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Program
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Session 1A:
Innovative Technologies
Physical
Mechanisms of Colloidal Silica Grouting in Remediation of
Chromium Contaminated Soil
Netnapid
Yossapol, New Jersey Institute of Technology, Newark, NJ
Reduction
of Leachable Dinitrotoluene Using Cement and Fly Ash
William B. Empson,
US Army Corp of Engineers, Kansas City, MO
In-Situ
Thermal Destruction Makes Stringent Soil and Sediment
Cleanup Goals Attainable
Ralph S. Baker,
TerraTherm, LLC, Fitchburg, MA
Physical
Mechanisms of Colloidal Silica Grouting in Remediation of
Chromium Contaminated Soil
Netnapid Yossapol and Prof. Jay N. Meegoda, New Jersey
Institute of Technology
The low-viscosity chemical grout, colloidal silica
(CS), is extensively used as a grouting material in
construction of grout curtains. CS with low viscosity and
non-toxicity is injected into soil to stabilize
fine-grained soils. It is also used as a viscous liquid
barrier in some hazardous waste sites (Persoff, 1995).
This paper presents a theoretical analysis of the
applicability of injected CS grouts to stabilize/solidify
chromium contaminated soils from Hudson County, NJ.
In this paper, physical mechanisms of CS grouting
treatment of chromium contaminated soil will be
investigated. During stabilization, after liquid CS is
injected into contaminated soil, it moves though the voids
inside soil matrix. The viscosity is increased while CS is
moving, causing a reduction of flow velocity in soil. The
above process results in thickening or coating of chromium
contaminated soil with CS by transforming liquid CS into a
gel. The gelling time and gelling mechanisms are
controlled by the variation in viscosity, which depends on
soil type, soil composition, concentration and chemical
characteristics of CS. The movement of CS during the
grouting process as a function of time, chemistry of grout
and environmental factors is modeled at the microscopic
level. The result will show the growth of film during
grouting process.
It is expected that the results from this study will
provide a theoretical basis for treatment of chromium
contaminated soils using CS grout. Moreover, this physical
model will provide design information for the real world
application of CS to stabilize chromium contaminated
soils.
Reduction
of Leachable Dinitrotoluene Using Cement and Fly Ash
William B. Empson and Jason M. Leibbert, U.S. Army
Corps of Engineers Kansas City District, David Hixson,
Jacobs Engineering Group, Raymond E. Bailey and Marjorie
Wesley, MK-Ferguson Company.
The former Weldon Spring Ordnance Works produced
Trinitrotoluene (TNT) and Dinitrotoluene (DNT) explosives
in the early 1940s. As a result of the manufacturing,
significant levels of explosives were present in site
soils. Efforts between 1945 and the 1960s to clean up
these explosives led to the co-mingling of explosives,
lead, and asbestos wastes. A portion of the site was used
by the Atomic Energy Commission (AEC) in the 1950s and
1960s for the processing of Uranium and Thorium. As a
result, some site soils contained both explosives and
radionuclides. The levels of 2,4 DNT in the soils were
determined to be greater than the regulatory limit of 130
m g/l under the Resource Conservation and Recovery Act (RCRA).
In order to facilitate disposal under the Land Disposal
Restrictions (LDRs), an innovative treatment method was
required since thermal treatment of soils containing
explosives and radionuclides or asbestos would be
exceptionally complicated. In a coordinated effort, the
Department of Energy (DOE) (Formerly AEC) was responsible
for any soils containing explosives and radionuclides
while the U.S. Army was responsible for any soils
containing explosives and lead or asbestos. Through bench
testing and strictly controlled field implementation, the
DOE determined that the addition of 20 percent by weight
cement and fly ash could reduce the leachable 2,4-DNT from
over 1000 m g/l to below the LDR limit of 130 m g/l. In
cooperation with the DOE, the U.S. Army Corps of Engineers
then expanded on the bench scale testing and implemented a
similar and equally successful field treatment operation
that demonstrated consistent compliance with the LDRs
using less rigorous field controls. The results of these
efforts indicate that the process is time dependent and
that temperature and water content affect the rate at
which the treatment process progressed. The process is
cost competitive with thermal treatment.
In-Situ
Thermal Destruction Makes Stringent Soil and Sediment
Cleanup Goals Attainable
Ralph S. Baker and John M. Bierschenk, TerraTherm, Inc.
In Situ Thermal Destruction (ISTD) is a soil and
sediment remediation process in which heat and vacuum are
applied simultaneously to subsurface soils or aboveground
soil/sediment piles. Heat flows into the soil primarily by
conduction from heaters typically operated at 700-800° C.
The heaters are installed in wells at regular intervals
within the soil. As soil is heated, organic contaminants
in the soil are vaporized or destroyed by several
mechanisms, including evaporation, steam distillation,
boiling, oxidation, and pyrolysis. The vaporized
constituents are drawn toward extraction wells for
aboveground treatment. Compared to fluid injection
processes, the conductive heating process during ISTD is
very uniform in its vertical and horizontal sweep. The
combined effectiveness of both heat and vapor flow leaves
no area untreated. Laboratory treatability studies and
field project experience at seven ISTD sites have
confirmed that high temperatures applied over a period of
days result in extremely high destruction and removal
efficiency of even high boiling point contaminants such as
PCBs, pesticides, PAHs and other heavy hydrocarbons. The
effectiveness of the process is not limited by the
presence of heterogeneous soil conditions or clay. Despite
high pre-treatment soil contaminant concentrations,
post-treatment soil concentrations have typically been
non-detect. Moreover, most of the contaminants (95-99% or
more) are destroyed in the soil before reaching the
surface. Stack sampling has demonstrated that emissions of
toxic air pollutants including dioxins are substantially
below standards. ISTD thus offers a cost-effective means
to reliably achieve stringent cleanup goals that have not
been previously possible by in-place treatment. The
implications for the setting of cleanup standards are
discussed.
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