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Beazer East, Inc.
Denver, Colorado, USA
Project
In Situ
Biogeochemical Stabilization (ISBS) of
Creosote/Pentachlorophenol NAPLS Using
Permanganate
Summary
A growing number of non-aqueous phase liquid
(NAPL) removal technologies have been promoted
commercially over the past few years,
including: thermal-enhanced recovery,
surfactant flooding, steam- and
temperature-enhanced extraction and others. It
is our experience that the effectiveness of the
NAPL removal is site-dependent and inversely
related to the NAPL saturation. Saturations
decline with each gallon on NAPL removed from
the formation until their residual saturation
is reached, where by definition NAPLs can no
longer flow to a well or trench. Although some
technologies may be capable of recovering a
small percentage of the residual NAPLs, it is
technically impracticable to recover a
significant percentage of the remaining
NAPLs.
The Challenge
At wood treating and related sites,
hydrocarbons may be present in the subsurface
as NAPLs.. These NAPLs tend to be a long-term
source of dissolved-phase organic plumes in
groundwater. NAPLs that are present in the
subsurface at saturations significantly above
their residual saturation can be removed by
enhanced recovery technologies; however, NAPLs
that are at or below their residual saturations
are trapped in the formation and are not
recoverable.
The Solution
An alternative approach to residual NAPL
recovery is in situ NAPL management. In situ
chemical oxidation for source area
stabilization entails the use of a permanganate
chemical oxidizer that is flushed through an
aquifer zone containing residual NAPLs. The
oxidant is not meant to remove NAPL mass
entirely. Rather, as the oxidant migrates
through the targeted source area,
(bio)geochemical reactions between the organic
constituents of interest (COIs) and the oxidant
cause the destruction and stabilization of NAPL
via a two step process: i) oxidation, and ii)
dissolution. The biochemical oxidation
processes destroy COIs present in the dissolved
phase, thereby increasing the dissolution of
COIs from the NAPL into the groundwater. The
more water soluble, lower-molecular-weight NAPL
constituents are then released and chemically
oxidized at a proportionally higher rate, thus
leading to a "hardening" or chemical
"weathering" of the residual NAPL mass. The
selective removal of the more labile
constituents causes a net increase in the
viscosity of the NAPL, yielding a more stable
NAPL source that is less susceptible to
dissolution processes. In addition, the
oxidation reaction precipitates manganese
dioxide (MnO2) and results in the formation of
a chemical "shell" which further isolates the
"weathered" NAPLs. As such, the flux of COIs
into the dissolved phase is decreased, allowing
natural attenuation processes to more
effectively manage COI plumes.
Proof of Concept
In 1997 scientists, now at Adventus,
conceptualized the ISBS technology and began
working on basic technology research and
development in collaboration with scientists at
the University of Waterloo. In 2002, pilot
scale field studies were initiated at an
operating wood treatment facility in Denver,
Colorado (Kopper's Inc., Superfund Site) where
24,050 gallons of 3% aqueous permanganate
(KMnO4) solution were injected into 13
locations within a defined test area (75 x 95 x
10 ft deep). Performance monitoring was
conducted for 6 months to evaluate the ability
of ISBS to stabilize the free-phase NAPL
residuals and enhance the natural attenuation
processes by: i) mitigating the migration of
NAPL; ii) reducing the concentration of COI in
the dissolved phase; iii) decreasing the mass
of NAPL residuals (source reduction); and iv)
reducing the flux of COI from NAPL residuals
(especially true with MnO2 precipitate). Field
data showed rapid and complete stabilization of
NAPL. In addition, mass was reduced by 10 to
79% (Table 1) and the flux of COI was reduced
by 56 to 99% (Table 2).
Table 1: Mass Reduction following a
Single ISBS Treatment - Denver,
CO.
|
COI (mg/kg)
|
Average (n=4)
Background
|
Average (n=4) Treated
|
% Mass Reduction
|
|
LMW PAHs
|
7,633.50
|
5,996.75
|
21
|
|
HMW PAHs
|
1,961.55
|
1,744.55
|
10
|
|
TOTAL PAHs
|
9,595.05
|
7,771.30
|
19
|
|
PENTA
|
236.00
|
55.67
|
76
|
|
TOTAL CPs
|
284.48
|
59.25
|
79
|
Table 2: Flux Reduction following a
Single ISBS Treatment - Denver,
CO
|
COI (mg/L)
|
Average (n=4)
Background
|
Average (n=4) Treated
|
% Flux Reduction
|
|
LMW PAHs
|
34.41
|
12.75
|
73
|
|
HMW PAHs
|
6.05
|
0.11
|
99
|
|
TOTAL PAHs
|
40.46
|
12.86
|
79
|
|
PENTA
|
18.91
|
9.66
|
49
|
|
TOTAL CPs
|
23.38
|
10.41
|
56
|
Table Legend: Tables 1 and 2 summarize the
results from pilot-scale field testing of ISBS
technology at the Kopper's Inc. Superfund Site
in Denver, CO where an area ca. 75,000 ft3 was
treated with modified per ISBS yielded a 53%
reduction in the residual mass of chlorinated
phenols (from 285.4 to 133.8 mg/kg) and a 19%
reduction in the mass of total PAHs (from 9,595
to 7,771 mg/kg). Decrease in Leachable
Constituents: Comparisons between the treated
and background samples indicated a 76% decrease
in the total PAH leachable (from the treated
soils). In the treated soils, the amount of
lower-molecular-weight (LMW) PAHs present in
the leachate was reduced by 73%;
higher-molecular-weight (HMW) PAHS were reduced
by more than 99% (percent flux reduction).
In December 2003, full scale application of
ISBS technology at the Denver Site was approved
by State of Colorado (CDPHE) and Federal (US
EPA Region VIII) regulators, following their
rigorous peer review (EPA Research
Laboratories) of all existing data. Full scale
application was completed in May 2004. A total
of 82,553 gal of KMnO4 @ 30 g/L Solution (3%)
was added to 44 injection points (Photo 1) and
9,789 gal were applied two three trenches (90
gal / LF trench) yielding a total 10,495 kg
KMnO4 for 4.5 g KMnO4 / Kg soil.
The Results
As applied to the Kopper's Inc. Superfund Site,
permanganate application had an effective
radius of influence of approximately 15 ft.
There was a discernible decrease over time in
the thickness of LNAPL for only those
monitoring piezometers located within the
permanganate treatment area. Changes in NAPL
thickness were not observed outside of the
treated area suggesting that NAPL migration did
not occur. Flux reduction should have a
significant beneficial affect thereby
accelerating the contraction of the dissolved
phase COI plume at the Kopper's Inc. Superfund
Site.
The Cost
The cost of full scale field implementation of
the ISBS technology was approximately $200,000.
As summarized below, this represents a very
cost-efficient, effective alternative for
managing NAPL sites.
Materials and Injection $11-15/cy
Drilling / Trenching $2-5/cy
Engineering $2-5/cy
TOTAL = $15 - 25/cy
Data exist to demonstrate that the ISBS
technology will effectively stabilize various
chlorinated solvents including
perchloroethylene (PCE), trichloroethylene
(TCE) and carbon tetrachloride (CT);
stabilization of hydrocarbons (creosote) and
chlorinated pesticides (i.e.,
pentachlorophenol) has also been documented
under field conditions. In-house data show that
technology will also stabilize certain metals
via the enhanced precipitation reactions. Since
January 2004, we have proposed the use of ISBS
technology for in situ source management
relatively large, complicated sites in South
Carolina (creosote), Florida (creosote),
Pennsylvania (chlorinated solvents), California
(chlorinated solvents), New Jersey (chlorinated
solvents), West Virginia (chlorinated
solvents), and New York (multiple MGP
sites).
References: Mike Tischuk, Mike Bollinger and
Mitchell Brourman (Beazer East, Inc., One
Oxford Center, Suite 3000, Pittsburgh, PA 15219
(412) 208-8800).
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