DNAPL Characterization and
Removal with Bioremediation Recirculation System and
Electrical Resistance Heating
Melinda
Montano, Shaw Environmental, Inc., Concord
,
CA
Vincent Chan, Shaw
Environmental, Inc., Concord
,
CA
Wayne Akiyama, Shaw
Environmental, Inc., Concord
,
CA
Dan Leigh, Shaw
Environmental, Inc., Concord
,
CA
Scott Anderson, U.S. Navy, San Diego, CA
Acetate
as the Sole Electron Donor, Concurrent Fe(III)
Rreduction, and the Prospect of Complete TCE
Dechlorination without Dehalococcoides
– New Concepts and Novel Data in Chlorinated Solvent
Bioremediation
Kevin T. Finneran, PhD, University of Illinois -
Urbana Champaign, Urbana, IL
A Comparison of Laboratory and
Field Data for Nutrient Amended Carbon Substrates
Michael R. Sieczkowski, CHMM, JRW Bioremediation L.L.C.,
Lenexa,
KS
Hexahydro-1,3,5-trinitro-1,3,5-triazine (RDX)Mechanisms
and Kinetics of Extracellular Electron Shuttle
Mediated Cyclic Nitramine (Biodegradation by a Novel
Bacterial Isolate)
Student Presenter
Man Jae Kwon,
University
of
Illinois
-
Urbana
Champaign,
Urbana, IL
Kevin T. Finneran, PhD,
University
of
Illinois
-
Urbana
Champaign, Urbana, IL
Full-Scale
Implementation of Bioremediation for PCE and TCE
Christopher Sullivan, Geosyntec
Consultants, Acton
,
MA
Carl Elder, Geosyntec
Consultants, Acton
,
MA
Douglas
Larson, Geosyntec Consultants, Acton
,
MA
Biodegradation of an MEK Ground
Water Plume over a Nine-Year Period
Richard D. Britton, The Whitman Companies,
Inc., East Brunswick,
NJ
Cheryl Coffee, Congoleum Corporation, Trenton, NJ
Michael Percelay
, The Whitman Companies,
Inc.,
East Brunswick
,
NJ
Keith McDermott, The Whitman Companies,
Inc.,
East Brunswick
,
NJ
DNAPL Characterization and
Removal with Bioremediation Recirculation System and
Electrical Resistance Heating
Melinda
Montano, Shaw Environmental, Inc.,
4005 Port Chicago Hwy,
Concord
,
CA
94520
,
USA
, Tel: 925-288-2216, Fax: 925-827-2029, Email:
melinda.montano@shawgrp.com
Vincent Chan, Shaw Environmental, Inc.,
4005 Port Chicago Hwy,
Concord
,
CA
94520
,
USA
, Tel: 925-288-2372, Fax: 925-288-0888, Email:
vincent.chan@shawgrp.com
Wayne Akiyama, Shaw Environmental, Inc.,
4005 Port Chicago Hwy,
Concord
,
CA
94520
,
USA
, Tel: 925-288-2003, Fax: 925-288-0888, Email:
wayne.akiyama@shawgrp.com
Dan Leigh, Shaw Environmental, Inc., 4005 Port Chicago
Hwy, Concord, CA 94520, USA, Tel: 925-288-2193, Fax:
925-288-0888, Email: daniel.leigh@shawgrp.com
Scott Anderson, U.S. Navy, 1455 Frazee Road, Suite
900, San Diego, CA 92108, USA, Tel: 619-532-0700,
Email: scott.d.anderson@navy.mil
A
source area of PCE has recently been identified as a
possible DNAPL plume at a site at Naval Station
Treasure Island. The
plume will be delineated using Membrane Interface
Probe (MIP) and FLUTe.
Then it will be treated using Electrical
Resistance Heating, or alternatively, using Enhanced
Solubility and Bioremediation.
Identification
of the DNAPL is based on groundwater sampling results
for an in situ bioremediation (ISB) system to treat
dissolved chlorinated ethenes.
The system consisted of injection and
extraction wells to distribute substrate and microbes
through recirculated groundwater.
The source area is at the tip of the plume,
which has not been comprehensively investigated.
Prior to treatment, the area had very high
concentrations, as determined by groundwater sampling
at well EW4. During
ISB, sampling showed substantially complete
dechlorination. After
treatment, sampling showed that concentrations had
rebounded to levels greater than 17,000 µg/L for
CVOCs. There
was no rebound in other areas, and the rebound
contaminant was mainly PCE, indicating that the PCE in
this area exists as DNAPL.
MIP
locations will be determined in a step-out pattern,
starting in the vicinity of EW4.
Depth of borings will be up to 35 ft bgs, or
the depth of the Bay Mud, which may be a confining
layer. The
results will be used to determine the desired
locations for FLUTe liners, and soil and groundwater
sampling. If
the presence of DNAPL is confirmed, it is expected to
take one of the following forms: 1) The form of pools,
which have low surface area to mass.
2) The form of small residual globules
disseminated through the aquifer, which have high
surface area to mass.
Treatment will be by Electrical Resistance
Heating or Enhanced Solubility and Bioremediation
depending on the form of the DNAPL.
Acetate
as the Sole Electron Donor, Concurrent Fe(III)
Rreduction, and the Prospect of Complete TCE
Dechlorination without Dehalococcoides
– New Concepts and Novel Data in Chlorinated Solvent
Bioremediation
Kevin T. Finneran, PhD,
University of Illinois - Urbana Champaign, Dept of
Civil and Environmental Engineering, NCEL 205 N.
Mathews, Urbana, IL, 61801, Tel: 217-333-1514, Fax:
217-333-6967, Email: finneran@illinois.edu
Trichloroethylene
(TCE) bioremediation has focused on reductive
dechlorination in most applications because of
prevalent anoxic, subsurface conditions that make
anaerobic metabolism favorable as opposed to aerobic
microbial metabolism.
There are several chlorinated solvent
bioremediation dogmas that in large part have
excellent data supporting them, but which at times
have had anecdotal data against them.
We began investigating two such remediation
tenets in detail.
The first is that acetate is a poor electron
donor for complete dechlorination.
Complete dechlorinators require H2 as the
primary electron donor, and acetate has to date only
been identified as a good carbon source for these
organisms. The
second widely held concept is that Fe(III) reduction
is a strictly competitive process, and that Fe(III)
must be fully reduced prior to the onset of cis-DCE or
VC reduction to generate ethene.
While investigating hypotheses related to these
concepts, molecular and physiological suggested
complete dechlorination without the presence of
Dehalococcoides microorganisms.
To date, these organisms are an absolute
requirement, and many engineered remediation
strategies are built on their presence or addition.
We
obtained TCE-contaminated aquifer material from a
confidential site in
Connecticut
. We began
two series of incubations using acetate as the sole
electron donor. The
first series had acetate present at 1:1 stoichiometric
concentration with respect to all electron acceptors (stoichiometric
batch). The
second series had acetate present at 10X the necessary
stoichiometry (10X batch), which is common practice in
engineered strategies as a “factor of safety”.
TCE in the stoichiometric batch was quickly
(<10 days) reduced to ethene without cis-DCE or VC
accumulation at near TCE:ethene stoichiometry.
VC was also reduced to ethene in the
stoichiometric batch when added as the primary
chlorinated solvent.
However, in the 10X batch, TCE was slowly
converted to ethene and reduction was incomplete (VC
accumulated and TCE:ethene was not stoichiometric).
These data suggest that lower, metered electron
donor addition, with acetate as the primary donor, can
stimulate efficient dechlorination.
Fe(III)
was concurrently reduced with ethene production in the
stoichiometric batch, where Fe(II) quickly spiked then
flattened in the 10X batch.
This demonstrates that stoichiometric electron
donor can stimulate overlapping respiratory processes,
most likely by increasing competition amongst the
populations present.
An added positive benefit was the lack of
methane in the stoichiometric batch, where methane was
produced up to 30µM in the 10X batch.
Methane is a potent greenhouse gas, and its
production needs to be limited in all remediation
applications.
Molecular
analysis using Dehalococcoides specific PCR primers
728F and 1172R demonstrated that DHE-like organisms
were not present in the aquifer material in any
incubation from which DNA was extracted (repeated
several times). Nested
PCR with universal Eubacterial primers and the DHE-specific
primers as the internal (nested) pair also
demonstrated lack of DHE-like molecular signatures.
Dehalococcoides ethenogenes strain FL2 was used
as a positive control in all molecular analyses, and
was repeatedly amplified using our techniques.
Amplified ribosomal 16S rDNA analysis (ARDRA)
using universal Eubacterial primers 338F and 907R did
not identify any DHE-like phylotypes in any of 900
clones tested. The
dominant genus identified in all sediment incubations
was within the genus Desulfosporosinus.
Preliminary data with liquid enrichment
cultures developed from this sediment indicate that
cultures are presented both with and without
Dehalococcoides. This
would be the first demonstration of complete
dechlorination (TCE ŕ
ethene) in the absence of Dehalococcoides, with
acetate as the sole electron donor.
Alternatively, it may also be the first
evidence of Dehalococcoides using acetate as the sole
electron donor.
A Comparison of Laboratory and Field Data for
Nutrient Amended Carbon Substrates
Michael R. Sieczkowski, CHMM, JRW
Bioremediation L.L.C., 14321 W 96th
Terrace,
Lenexa
,
Kansas
66215
,
USA
, Office (913) 438-5544 extension 122, Fax (913)
438-5554, msieczkowski@jrwbiorem.com
The use of enhanced reductive
dechlorination through the addition of carbon
substrates has become a common remedial option for
chlorinated solvents since the mid-1990s.
Since that time, many types of carbon
substrates have been developed and tested with varied,
but mostly positive results.
The use of a wide variety of substrates was
driven predominantly by both substrate and application
cost. This
led to the use of less expensive, non-engineered
substrates. This
paradigm shift resulted in a shift in the relative
cost of the substrate when compared to the total site
cost. Highly
engineered substrates could account for more than 60%
of the total cost of site work whereas non-engineered
substrates generally account for a much lower
percentage, in some cases as low as 25% of the total
cost of site work.
In their efforts to further
reduce total project costs, the industry looked at
increasing degradation efficiency by augmenting
systems with microbes specifically designed to degrade
target contaminants or through the addition of
nutrients. Although
microbial bioaugmentation can be successful, in many
cases it does not produce a reduction in total project
costs significant enough to warrant wide-spread use.
Nutrient addition likewise was not generally
seen to dramatically impact overall costs on most
sites.
Similar to the move to develop
more cost effective substrates, work to develop more
cost effective nutrients has been a common goal.
Recent breakthroughs in the development of less
costly nutrients (in some cases by more than two
orders of magnitude) have made nutrient addition more
economically viable.
This presentation reviews laboratory microcosm
studies on a nutrient designed to increase anaerobic
microbial efficiency and kinetics while reducing
overall costs. These
results are then compared to in situ pilot field
trails using a variety of carbon substrates including
whey powder, ethyl lactate, and emulsified vegetable
oil.
Hexahydro-1,3,5-trinitro-1,3,5-triazine
(RDX)Mechanisms and Kinetics of Extracellular Electron
Shuttle Mediated Cyclic Nitramine (Biodegradation by
a Novel Bacterial Isolate)
Student Presenter
Man Jae Kwon,
University of Illinois - Urbana Champaign, Dept of
Civil and Environmental Engineering, NCEL 205 N.
Mathews, Urbana, IL, 61801, Tel: 217-333-6851, Fax:
217-333-6967, Email: mankwon@uiuc.edu
Kevin
T. Finneran, PhD, University of Illinois - Urbana
Champaign, Dept of Civil and Environmental
Engineering, NCEL 205 N. Mathews, Urbana, IL, 61801,
Tel: 217-333-1514, Fax: 217-333-6967, Email: finneran@uiuc.edu
A cyclic nitramine explosive,
hexahydro-1,3,5-trinitro-1,3,5-triazine (RDX),
is a contaminant of concern at many military sites and
live-fire training installations(Spalding and Fulton,
1988; Haas et al., 1990).
Groundwater contaminated by RDX is of growing
environmental concern because of human health effects
of RDX. The current study investigated the potential
of utilizing indigenous microorganisms for in situ RDX
bioremediation.
Microbial enrichments were
generated using RDX-contaminated aquifer material that
was incubated with a variety of electron donors and
acceptors. Electron donors tested included H2,
benzoate, formate, lactate, or acetate; electron
acceptors included poorly crystalline Fe(III) oxide,
or RDX. Approximately 60% of RDX was mineralized to
CO2 in the cell suspension of the enrichment cultures
incubated with lactate or acetate.
A new bacterial species, MJ1, was
enriched from the same aquifer material and isolated
by streaking on an anaerobic agar slant with RDX as
the sole electron acceptor.
The MJ1 colony was translucent, viscous, and of
convex and circular shape with a size range of 1-2mm.
The full 16S rRNA gene sequence of MJ1 showed that it
is a novel species in the genus Desulfotomaculum. 16S
rRNA phylogenetic cluster analysis demonstrated that
MJ1 is closely related to species in Geobacteraceae,
Shewanella, and Anaeromyxobacter, which have been
shown to reduce RDX as well as Fe(III). MJ1 showed
gram-negative staining behavior. However, cell walls
of Desulfotomaculum, in general, contain the typical
ultrastructure of gram-positive bacteria. MJ1 is
rod-shaped. The optimal growth temperature and pH of
MJ1 with Fe(III) and acetate were 30°C and 7, respectively. Electron donors utilized with Fe(III)
were lactate, acetate, formate, ethanol, H2, benzoate.
Electron acceptors utilized with acetate were Fe(III),
fumarate, and AQDS. A preliminary experiment
demonstrated that MJ1 under growth condition reduced
RDX below the detection limit within 7 days. This
isolate will be characterized further with respect to
RDX transformation in detail.
Full-Scale
Implementation of Bioremediation for PCE and TCE
Christopher Sullivan, Geosyntec Consultants,
289 Great Rd, Suite 105
,
Acton
,
MA
01720
, Tel: 978-263-9588, Fax: 978-263-9594, Email: csullivan@geosyntec.com
Carl Elder, Geosyntec Consultants,
289 Great Rd, Suite 105
,
Acton
,
MA
01720
, Tel: 978-263-9588, Fax: 978-263-9594, Email: celder@geosyntec.com
Douglas Larson, Geosyntec Consultants,
289 Great Rd, Suite 105
,
Acton
,
MA
01720
, Tel: 978-263-9588, Fax: 978-263-9594, Email: dlarson@geosyntec.com
This
presentation describes the design, implementation, and
operation of a full-scale bioaugmentation remedy over
the 3.5 acre site that is the source to a 3500 foot
plume. Particular
focus is given to the accomplishments achieved during
the last five years and lessons learned from this
project
The
site is a former manufacturing plant in
Kansas
. Site
geology consists of approximately 35 feet of fine sand
underlain by limestone bedrock.
Groundwater is located approximately 15 feet
below the ground surface.
Prior to implementing bioremediation,
overburden groundwater was slightly oxidizing and
aerobic (ORP = +200 mV, DO = 5 mg/l) with average
nitrate and sulfate concentrations of approximately 7
and 25 mg/L, respectively.
Concentrations of PCE and TCE in site
groundwater were initially as high as 2 mg/L and 11
mg/L, respectively.
Bioremediation
was proposed in 2003 as an alternative to pump and
treat for the source area.
A bioremediation system consisting of two
groundwater extraction wells, a treatment trailer and
four injection wells was designed, permitted and
installed in the Spring of 2004.
Full-scale operation of the bioremediation
system began in July 2004.
Groundwater
was initially amended with acetate to achieve iron
reducing conditions.
After four months of operation, the electron
donor was changed to lactate to maintain strongly
reducing conditions.
The site was bioaugmented with KB-1™ in
January and November 2005 (approximately six and
sixteen months after system start-up).
The system has operated continuously since July
2004 at a pumping rate of approximately 12 gpm and
lactate dose of about 130 mg/L (since November 2004).
Bioremediation
has destroyed approximately 99% of the mass within the
treatment zone and more than 80% of the contaminant
mass site-wide. Nearly
all of the remaining contaminant mass is located in a
zone up gradient of the bioremediation system that was
discovered after 2004. PCE
and TCE concentrations within the treatment zone on
the western half of the site have decreased from
approximately 2 mg/L to drinking water levels.
Concentrations on the eastern half of the site
have decreased from as much as 10 mg/L to drinking
water levels with the exception of two localized
hotspots where TCE concentrations are approximately
100 ug/L. Bioremediation
has resulted in sufficient mass removal for the state
regulators to approve reactivation of a municipal
supply well that is located at the down gradient
boundary of the site.
This well was deactivated in 1985 as a result
of site contamination.
In August 2008, 500 gallons of emulsified
soybean oil was added at select locations throughout
the site to provide a persistent source of electron
donor for bioremediation of residual contamination and
the active treatment system was shutdown.
Biodegradation of an MEK Ground Water Plume over a
Nine-Year Period
Richard D. Britton, The Whitman Companies,
Inc.
116 Tices Lane
, Unit B-1,
East Brunswick
,
NJ
08816
, Tel: 732-390-5858, Fax: 732-390-9496, Email: rbritton@whitmanco.com
Cheryl Coffee
, Congoleum Corporation.
1945 East State Street
,
Trenton
,
New Jersey
08619
, Tel: 609-584-3000, Fax: 609-584-3300, Email: ccoffee@congoleum.com
Michael Percelay
, The Whitman Companies, Inc.
116 Tices Lane
, Unit B-1,
East Brunswick
,
New Jersey
,
08816
, Tel: Fax: 732-390-5858, 732-390-9496, Email: mpercelay@whitmanco.com
Keith McDermott
, The Whitman Companies, Inc.
116 Tices Lane, Unit B-1, East Brunswick, New
Jersey, 08816, Tel: 732-390-5858, Fax: 732-390-9496,
Email: kmcdermott@whitmanco.com
Methyl Ethyl Ketone (MEK)
concentrations at an industrial facility located in
Central, New Jersey (NJ) naturally degraded from
concentrations of 354,000 ppm to ND (
<
10 ppb) between 1998 and 2007.
In 1999, the maximum area of MEK
concentrations that exceeded the NJ MEK ground water
quality criterion of 300 ppb reached approximately
100,000 square feet.
Saturated subsurface materials (DTW=3.5
feet bgs) at the site are comprised primarily of fine
to medium sand with a hydraulic conductivity of 4.7 x
10-3 cm/sec.
Between 1998 and 2005, dissolved
oxygen (DO) concentrations at the source area and
other nearby monitoring wells were 0.0 mg/l,
indicating that microorganisms were actively degrading
MEK. DO
concentrations in source area wells began to rise in
2005 and rebounded to approximately 5 mg/l by 2007.
The timeframe for MEK to
concentrations to degrade below the NJ ground water
quality criterion of 300 ppb would have been predicted
to be much shorter than nine years given the
literature half-life values of 28 days and 7 days for
anaerobic and aerobic biodegradation of MEK.
The persistence of elevated MEK concentrations
suggested the presence of unremediated residual source
material.
A 2004 investigation in the
vicinity of the source area monitoring wells employing
a hydrophobic dye (Sudan IV) and FLUTe liners
identified a 1500 square feet area of free-phase
residual product near the initial discharge area.
It is believed that the rapid
decrease in MEK concentrations observed during late
2005 is correlated with the final dissolution of the
identified pockets of residual product.
Given the absence of any
sensitive receptors, and a stable then shrinking
ground water plume, natural attenuation was the most
appropriate and cost effective remedial action to
reach the NJ MEK ground water quality criteria of 300
ppb.