Bioremediation of Dual Contaminant Mixtures: TCE and RDX
Travis
S.M. Young, University of Nebraska Lincoln, Lincoln, NE
Matthew C. Morley, University of Nebraska Lincoln,
Lincoln, NE
Daniel D. Snow, University of Nebraska Lincoln, Lincoln,
NE
A
Kinetic Model of Reductive TNT Transformation by Escherichia
coli Resting Cells
Hong
Yin, University of Connecticut, Storrs, CT
Thomas K. Wood, University of Connecticut, Storrs, CT
Barth F. Smets, University of Connecticut, Storrs, CT
Combined
Anaerobic Oxidation and Reductive Dechlorination for
Optimizing Bioremediation of CVOCs: Theoretical and
Practical Considerations
Eric C. Hince, Geovation Technologies, Inc., Florida, NY
Evaluation
of Biological Treatment Options for N-Nitrosodimethylamine
(NDMA) in Groundwater
Paul
B. Hatzinger, Shaw Environmental, Inc., Lawrenceville, NJ
Sheryl Streger, Shaw Environmental, Inc., Lawrenceville,
NJ
Kevin McClay, Shaw Environmental, Inc., Lawrenceville, NJ
Robert J. Steffan, Shaw Environmental, Inc.,
Lawrenceville, NJ
Treatment
of Vinyl Chloride Contaminated Groundwater at a Landfill
Site: Comparison of Biosparging and iSOC™ Bioremediation
Systems for Plume Cut-off
Christine
R. LeBlanc, East Coast Engineering, Inc., Marion,
MA
James
F. Begley, MT Environmental Restoration, Plymouth, MA
Treatment
of PCP-Contaminated Soil Using an Engineered Ex Situ
Biopile Process at a Superfund Site
Carl
Rodzewich, Biogenie Corporation, Quakertown, PA
Nile Fellows, Minnesota Pollution Control Agency, St.
Paul, MN
Nicolas Moreau, Biogenie Corporation, Quakertown, PA
Michel Pouliot, Biogenie Corporation, Quakertown, PA
A
Comprehensive Performance Analysis of Hydrogen Release
Compound (HRC®): Lessons
Learned and Future Directions
Anna
Willett, Regenesis, San Clemente, CA
Stephen S. Koenigsberg, San Clemente, CA
Bioremediation
of Dual Contaminant Mixtures: TCE and RDX
Travis
S.M. Young, Department of Civil Engineering, University of
Nebraska Lincoln, Lincoln, NE 68588-0531, Tel:
402-472-5026, Fax: 402-472-8934, Email:
travisy74@yahoo.com
Matthew C. Morley, Department of Civil Engineering,
University of Nebraska Lincoln, Lincoln, NE 68588-0531,
Tel: 402-472-2057, Fax: 402-472-8934, Email:
mmorley2@unl.edu
Daniel D. Snow, Water Sciences Laboratory, 103 Natural
Resources Hall, University of Nebraska-Lincoln, Lincoln,
NE 68583-0844, Tel: 402-472-7539, Fax: 402-472-9599,
Email: dsnow1@unl.edu
High
explosives and chlorinated solvents are common soil and
groundwater contaminants at numerous military facilities
worldwide. One such site is the former Nebraska Ordnance
Plant (Mead, NE), which has areas of contaminated
groundwater with both trichloroethylene (TCE) and RDX
(hexahydro-1,3,5-trinitro-1,3,5-triazocine). Contaminated
groundwater is currently extracted and treated using
ex-situ adsorption to granular activated carbon (GAC).
Bioremediation of this contaminant mixture is a potential
alternative for treating groundwater at the site, as
numerous studies have found that these contaminants are
amenable to biological transformation under reducing
conditions. In the present study, two cultures are being
tested for biodegradation potential: anaerobic digester
sludge from a municipal wastewater treatment plant, and a
facultative culture enriched from solids backwashed from
GAC contactors exposed to TCE- and RDX-contaminated
groundwater. With no prior exposure to RDX, both cultures
biodegraded RDX in single-component tests under anaerobic
conditions. RDX concentrations decreased rapidly with
evidence for transient production of nitroso-RDX
metabolites. The culture enriched from the backwash solids
degraded RDX at a much faster rate than the anaerobic
sewage sludge. Unacclimated
anaerobic sludge did not transform TCE during initial
10-day batch tests. Both cultures are currently being
grown in the presence of TCE, and additional tests will
determine if the acclimated cultures can biodegrade TCE
and mixtures of TCE and RDX. Successful biodegradation of
this contaminant mixture will yield a new remedial option
that can reduce the required time and costs for
remediating this contaminant mixture.
A
Kinetic Model of Reductive TNT Transformation by Escherichia
coli Resting Cells
Hong
Yin, Environmental Engineering Program, University of
Connecticut, 261 Glenbrook Road, Storrs, CT 06269-2037,
Tel: 860-486-0583, Fax: 860-486-2298, Email:
yinh@engr.uconn.edu
Thomas
K. Wood, Department of Chemical Engineering &
Molecular and Cell Biology, University of Connecticut, 191
Auditorium Road, Storrs, CT 06269-3222, Tel:
860-486-2483
, Fax:
860-486-2959, Email: twood@ngr.uconn.edu
Barth F. Smets, Dept of Civil and Environmental
Engineering & Molecular and Cell Biology, University
of Connecticut, 261 Glenbrook Road, Storrs, CT
06269-2037,Tel: 860-486-2270, Fax: 860-486-2298, Email: barth.smets@uconn.edu
TNT
biotransformation via nitro-reduction may be harnessed for
bioremediation of hazardous waste sites. However, these
transformations have been poorly understood or modeled.
Traditional Michaelis-Menten model does not describe the
nitro-reduction kinetics due to product toxicity and
reducing power limitation experienced by cells. In this
paper, TNT transformation by Escherichia coli was
monitored and a kinetic model for TNT depletion was
developed and experimentally calibrated. Using resting
cells of aerobically pregrown Escherichia coli,
2,4,6-trinitrotoluene (TNT) was transformed via
hydroxylaminodinitrotoluenes (2HADNT, 4HADNT, with 4HADNT
as the dominant isomer) to 2,4-diamino-6-nitrotoluene
(24DA6NT) as final product. Factors controlling the TNT
transformation were quantified, including enzyme
concentration, substrate concentration, and exogenous
reducing power concentration. At higher cell densities, or
by supplying glycerol as exogenous reducing power source,
the rate and extent of TNT reduction increased revealing
the importance of enzyme concentration and reducing power.
Product toxicity (resulting from toxicity of TNT
transformation intermediates) was quantified. A
comprehensive model incorporating reducing power
limitation, product toxicity, substrate inhibition, as
well as substrate limitation adequately described the
experimental observations.
Combined
Anaerobic Oxidation and Reductive Dechlorination for
Optimizing Bioremediation of CVOCs: Theoretical and
Practical Considerations
Eric
C. Hince, P.G., Geovation Technologies, Inc., 468 Route
17A, Florida, NY, 10921, Tel:
845-651-4141, Fax: 845-651-0040, Email: echince@geovation.com
In-situ
anaerobic bioremediation has become a preferred remedy for
ground-water contaminated with chlorinated solvents (CVOCs).
Most anaerobic bioremediation programs for CVOCs
have focused on driving classical reductive dechlorination
via the addition of carbon substrates (electron donors),
bioaugmentation with Dehalococcoides cultures or
both. Relatively
few examples of anaerobic oxidation processes have been
demonstrated for CVOCs, either alone or in combination
with reductive dechlorination.
Anaerobic oxidation processes coupled to the
microbial reduction of electron acceptors such as nitrate,
Mn(IV), Fe(III), and sulfate under anaerobic conditions
may offer alternate catabolic pathways for CVOCs that may
compliment reductive dechlorination. For example, reductive dechlorination may proceed rapidly for
highly chlorinated compounds such as PCE, TCE and
1,1,1-TCA and help activate these compounds for further
degradation, whereas anaerobic oxidation processes may be
more effective for less-chlorinated intermediates such as
cDCE and vinyl chloride.
In addition, combined anaerobic oxidation-reduction
treatment may help accelerate bioremediation by (a)
improving electron flow and regenerating oxidants and
reductants; (b) enhancing the biological removal of
intermediates and byproducts of substrate-enhanced
anaerobic treatment; and (c) promoting a broader array of
catabolic processes than can directly or indirectly attack
CVOCs and their daughter products.
Accordingly, the combination of anaerobic reduction
and oxidation processes should provide means for improving
and optimizing the anaerobic bioremediation of CVOCs,
particularly for source areas of contamination. Sites with large amounts of non-aqueous-phase contamination,
(i.e., those that may require long-term treatment), may
particularly benefit from this approach. Practical
considerations for the assessment and implementation of
combined anaerobic oxidation-reduction programs will be
discussed, and data from ongoing anaerobic bioremediation
programs will be presented to illustrate the efficacy and
potential of this approach for CVOC source-area
remediation.
Evaluation
of Biological Treatment Options for N-Nitrosodimethylamine
(NDMA) in Groundwater
Paul
B. Hatzinger, Ph.D., Princeton Research Center, Shaw
Environmental, Inc., 4100 Quakerbridge Road,
Lawrenceville, NJ 08648, Tel: 609-936-9300, Fax:
609-936-9221, Email: paul.hatzinger@shawgrp.com
Sheryl Streger, Princeton Research Center, Shaw
Environmental, Inc., 4100 Quakerbridge Road,
Lawrenceville, NJ 08648, Tel: 609-936-9300, Fax:
609-936-9221, Email: sheryl.streger@shawgrp.com
Kevin McClay, Princeton Research Center, Shaw
Environmental, Inc., 4100 Quakerbridge Road,
Lawrenceville, NJ 08648, Tel: 609-936-9300, Fax:
609-936-9221, Email: kevin.mcclay@shawgrp.com
Robert J. Steffan, Ph.D., Princeton Research Center, Shaw
Environmental, Inc., 4100 Quakerbridge Road,
Lawrenceville, NJ 08648, Tel: 609-936-9300, Fax:
609-936-9221, Email: robert.steffan@shawgrp.com
N-Nitrosodimethylamine
(NDMA) is a potent carcinogen and an emerging groundwater
contaminant. The
origin of NDMA in groundwater and drinking water includes
industrial, agricultural, water treatment, and military
sources.
The objective of this project was to evaluate
possible bioremediation strategies for treating NDMA-contaminated
groundwater. Our
initial studies revealed that the propane-oxidizing strain
Rhodococcus ruber ENV425 cometabolically degraded NDMA. The
toluene-oxidizing strains, Pseudomonas
mendocina KR1 and Pseudomonas
sp. ENVPC5, each of which contains toluene-4-monoxygenase
(T4MO) were also observed to degrade NDMA.
In addition, rapid removal of NDMA was achieved
using a P. putida
strain containing cloned T4MO, further demonstrating the
role of T4MO in NDMA degradation. To evaluate the
potential for ex situ biological treatment of NDMA, a chemostat was seeded with P.
mendocina KR1 and continuously fed toluene (~ 2 g/day)
as a primary substrate.
After establishing the culture at a dilution rate
of 0.02 hr-1,
NDMA was fed to the reactor at concentrations
ranging from 25 to 250 mg/L, to represent typical
groundwater concentrations. Strain
KR1 consistently degraded NDMA to below 0.2 mg/L during
the 4-month study. In
addition to the reactor studies, the potential for in
situ treatment of NDMA was examined using groundwater
samples from a contaminated site in California. The
addition of toluene, propane, and methane to microcosms
prepared with these samples was not effective for
stimulating indigenous organisms to cometabolize NDMA.
However, appreciable losses of NDMA was observed in
groundwater augmented with R.
ruber ENV425 in the presence or absence of propane as
a cosubstrate. The results from this research provide a
firm basis for the development of in
situ and ex situ biological approaches for NDMA remediation.
Treatment
of Vinyl Chloride Contaminated Groundwater at a Landfill
Site: Comparison of Biosparging and iSOC™ Bioremediation
Systems for Plume Cut-off
Christine
R. LeBlanc, East Coast Engineering, Inc., 156A Front
Street, PO
Box 745, Marion, MA 02738, Tel:
508-748-2460, Fax: 508-748-2553, Email: cleblanc@eastcoastengineering.com
James F. Begley, MT Environmental Restoration, 24 Bay View
Avenue, Plymouth, MA 02360, Tel: 508-732-0121, Fax:
508-732-0122, Email: jbegley@cape.com
Persistent
vinyl chloride plumes resulting from incomplete reductive
dechlorination of chlorinated solvents in groundwater
downgradient of landfill and dry cleaner sites often
present significant risk to drinking water resources and
potentially to indoor air quality.
A groundwater remediation program designed to treat
a large deep vinyl chloride plume (85 ft below the water
table) was implemented in June 2003 downgradient of a
former landfill site in Massachusetts.
Response actions selected for the site include a
system for vinyl chloride hot spot treatment by direct
aerobic biostimulation using biosparging and iSOC™ (in-situ
Submerged Oxygen Curtain) technology.
iSOC™ is an in situ
bioremediation/natural attenuation enhancement substrate
delivery system. The
iSOC™ unit provides a large surface area for delivery of oxygen by
mass transfer from the gas phase to the dissolved phase in
groundwater without sparging.
Initial
performance monitoring results have indicated that oxygen
delivery is effectively stimulating aerobic bacteria and
reducing vinyl chloride concentrations. Dissolved oxygen has increased from less than 1 mg/L to 11
mg/L in the biosparging treatment zone.
Dissolved oxygen concentrations as high as 130 mg/L
have been achieved in iSOC™ treatment wells and the
concentration of vinyl chloride within the active iSOC™
treatment zone has been reduced to 3 to 4 ug/L from a
baseline concentration of 10 to 15 ug/L.
The presentation will include an evaluation of
treatment zones developed by the biosparging and iSOC™
systems, system performance, and the design, development,
and optimization of aerobic treatment zones for plume
cut-off.
Treatment
of PCP-Contaminated Soil Using an Engineered Ex Situ
Biopile Process at a Superfund Site
Carl
Rodzewich, Biogenie Corporation, 2085 Quaker Pointe Drive,
Quakertown, PA 18951,
Tel: 215-538-1729, Fax: 215-538-8287, Email: crodzewich@biogenie-env.com
Nile Fellows, Minnesota Pollution Control Agency, 520
Lafayette Road, St. Paul, MN, 55155, Tel: 651-296-7299,
Fax: 651-296-9707, Email: nile.fellows@pca.state.mn.us
Nicolas Moreau, Biogenie Corporation, 2085 Quaker Pointe
Drive, Quakertown, PA
18951, Tel: 215-538-1729, Fax: 215-538-8287, Email:
nmoreau@biogenie-env.com
Michel Pouliot, Biogenie Corporation, 2085 Quaker Pointe
Drive, Quakertown, PA
18951, Tel: 215-538-1729, Fax: 215-538-8287, Email:
mpouliot@biogenie-env.com
Releases
of creosote and pentachlorophenol (PCP) at a New Brighton,
Minnesota wood treatment facility, resulted in widespread
soil and groundwater contamination.
Site investigations lead to the facility’s
inclusion on the National Priorities List (NPL), and the
Minnesota Pollution Control Agency was designated lead
regulatory agency. Biological
treatment was the preferred remedy for 18,000 yd³ of
contaminated soil, and Biogenie was contracted to design,
construct and operate an ex situ Biopile to achieve
the remedial objectives.
Most project owners and remedial managers perceive
the Biopile process as a passive remediation technology,
not fully appreciating the scientific and engineering
expertise required to design and operate an effective
Biopile. This
paper highlights the “behind the scenes” efforts of
the scientific and engineering team responsible for the
Biopile project, and specifically how those efforts
achieved difficult remedial objectives within a treatment
performance guarantee contract.
The
New Brighton project required that an ex situ
Biopile be used to achieve site reuse criteria of 10 mg/kg
PCP and 5 mg/kg cPAHs, with a schedule dictating operation
during winter months reaching -22°C. Biopile operating
parameters were developed during laboratory Treatability
Studies (TS) designed to optimize the biodegradation
capacity of indigenous microorganisms. Specific
operational parameters were also devised to manage soil
containing a fair proportion of highly impacted woodchips.
An engineering team applied the TS results during scale-up
Biopile design and the project team mobilized to the site
for construction. Once
operational the cleanup objectives were met within 18 to
38 weeks, depending on initial PCP concentrations which
were up to 350 mg/kg.
Average PCP reduction rates achieved 95% for soils
and 76% for soils containing wood chips.
With
appropriate design and operating parameters, the
engineered ex situ Biopile process enabled more
than 96% of the total volume of soil to be successfully
treated and backfilled on site, thus significantly
reducing overall project costs.
A
Comprehensive Performance Analysis of Hydrogen Release
Compound (HRC®): Lessons
Learned and Future Directions
Anna
Willett, Regenesis, 1011 Calle Sombra, San Clemente, CA
92673, Tel: 949-366-8000, Fax: 949-366-8090, Email:
awillett@regenesis.com
Stephen S. Koenigsberg, 1011 Calle Sombra, San Clemente,
CA 92673,
Tel: 949-366-8000, Fax: 949-366-8090, Email: skoenigsberg@regenesis.com
Since
1999, Hydrogen Release Compound (HRC®) has
been a commercially-available product for engineered
bioremediation of anaerobically biodegradable
contaminants. HRC
is a polylactate ester that, upon hydration or microbial
cleavage of its ester bonds, slowly releases lactate.
Lactate serves as an electron donor and carbon
source for microbial reductive biodegradation.
HRC is a viscous amber-colored liquid that is
typically injected into a contaminated aquifer using
direct push technology or backfill injection via a hollow
stem auger. Once
in place, HRC creates a plume of lactate and its
fermentation products (dissolved hydrogen and other
organic acids) downgradient of the injection area and
serves to accelerate anaerobic bioremediation processes.
In
this review of HRC field application results, we summarize
application types, contaminants treated, site types,
application locations, injection methods, site lithology
and hydrology, and concentration ranges of geochemical
species. The
source of this information is a database of 474 HRC field
applications, a series of 66 HRC publications (many by
independent authors), and 10 detailed site case histories
that are available electronically.
We will also address the overarching issue of
incomplete dechlorination and discuss how the cause of
incomplete dechlorination can be “diagnosed” and a
remedy implemented.
First
and foremost, the hidden mass input from desorption of
soil-phase contaminants and dissolution of residual DNAPL
should be considered significant factors in an apparent
slow down of dechlorination.
Additionally, competing electron acceptors such as
ferric iron can have a significant effect on the rate of
dechlorination. For
sites with these behaviors, we recommend, “more time and
more electrons.” On
the other hand, if sufficient electron donor is present,
but phylogenetic DNA tests show that the appropriate
microbial community is not present in sufficient numbers,
bioaugmentation with a dechlorinating inoculum is an
appropriate remedy. Site examples with monitoring data will be used to support
these conclusions.
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