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Stephen S.
Koenigsberg, Regenesis, San Clemente, CA
(steve@regenesis.com)
William R.
Mahaffey, Pelorus, Evergreen, CO
(mahaffwr@worldnet.att.net)
Introduction
As a ubiquitous fuel additive,
methyl tert-butyl ether (MTBE), has complicated the
remediation and closure of contaminated properties.
Regulators, oil companies, and now the public are becoming
increasingly concerned about the environmental impact of this
and other related ether oxygenates. Several factors
responsible for the heightened level of concern include the
following: 1) MTBE degrades very slowly under aerobic
conditions, 2) it has a very low taste and odor threshold, 3)
its toxicity and carcinogenicity profile are largely
undetermined and 4) it is highly soluble and does not readily
retard on the aquifer matrix. This last feature has
compromised active remediation methods (air sparging and pump
and treat) because of inefficiencies in stripping. As a
result, many consultants have turned to other treatment
options – most notably in-situ aerobic bioremediation.
Active in-situ aerobic
bioremediation, designed to accelerate rates of natural
attenuation, requires supplemental oxygen. One option in
achieving this is the use Oxygen Release Compound (ORC).
Oxygen Release Compound is patented formulation of
time-release magnesium peroxide that releases oxygen slowly
when hydrated. ORC treatment represents a “low intensity”
approach to in-situ aerobic bioremediation; it is simple to
apply, operates passively and is very low in cost because its
use dramatically limits design, capital and operating
expenses. One application of ORC typically lasts 6 months to
one year depending on site conditions. Its ability reduce time
to site closure has been intensively documented via its use at
6,500 sites in 50 states and 12 countries. There is also a
full body of independent, peer reviewed literature on its
performance which can be accessed at
www.regenesis.com.
ORC is applied using
exchangeable filter socks or as a loose powder. Filter socks
are placed in an array of wells or trenches, after which
contact with ground water promotes the formation of an “oxygen
barrier” that facilitates plume cut-off. ORC powder can be
made into a slurry for permanent applications in the saturated
zone, or dispersed as free powder for the in-situ or ex-situ
treatment of soil. A broad array of treatment points, in which
ORC slurry is backfilled or injected, can be implemented with
low-cost, small-bore injection or auguring methods. Loose
powder is traditionally used in the remediation of residual
contamination at the bottom of tank excavations. The first and
most dominant applications of ORC were for the treatment of
BTEX compounds and other petroleum hydrocarbons. Use has now
expanded to the remediation of certain chlorinated compounds,
such as vinyl chloride and ethers such as MTBE. A more
complete review of the technology can be found in Koenigsberg
and Sandefur (1999).
Establishing the Efficacy of
ORC in the Field
The observation that ORC could
be used in the treatment of MTBE came fortuitously. In 1996,
at a time when MTBE was not being regulated, we would
encounter an occasional consultant who would be particularly
thorough and analyze groundwater for “everything”. As a
result, MTBE levels would sometimes be reported in conjunction
with conventional BTEX and TPH data in the course of tracking
the performance of ORC. When we investigated the issue more
closely we realized that MTBE was a potential concern and that
it was degrading at a faster rate than would be expected in
accordance with published rates (Howard et al., 1991). These
data represent the exposure of the contaminants to fairly high
levels of dissolved oxygen (20-30 ppm), in wells where ORC
socks were being applied. Combined with the fact that
stripping is not possible, especially with a slow release of
oxygen, the hypothesis emerged that ORC was facilitating the
aerobic bioremediation of MTBE by increasing levels of
dissolved oxygen in the aquifer. This hypothesis was
formulated in large part due to the foundation work of
Salanitro et al., (1994) in which it was shown that a
bacterial consortium was capable of complete aerobic
degradation of MTBE. This work in turn was founded on a
variety of reports involving the aerobic degradation of other
ethers and a series of inconclusive studies pertaining to the
aerobic and anaerobic degradation of MTBE itself.
Subsequent to these field
observations, which were reported by Koenigsberg (1997), other
oxygen-mediated bioremediation field evidence appeared in
presentations by Javanmardian and Glaser (1997) and by Carter
et al., (1997). These studies reported remediation of MTBE by
air and oxygen sparging respectively. Following this, as MTBE
became more of a regulatory concern, other data sets
supporting the hypothesis that ORC could facilitate the
remediation of MTBE were being accumulated.
Supporting the Field
Observations with Laboratory Results
Subsequent to the work of
Salanitro et al., (1994) which presented the more general
evidence for the role of aerobic processes, there was a
specific report by Park and Cowan (1997) which established and
quantified a clear link between oxygen in the bioremediation
of MTBE. As a result, Regenesis commissioned studies at the
University of California at Riverside with Marc Deshusses and
Nathalie Fortin to corroborate these findings. The intent was
to offer some evidence, under controlled conditions, that
oxygen indeed was the limiting factor in the rate of MTBE
biodegradation. The studies as reported in Koenigsberg et al.,
(1999) investigated the biodegradation of MTBE by respirometry.
In the experiment, oxygen uptake rates at various dissolved
oxygen concentrations were used to quantify the influence of
dissolved oxygen concentration on the rate of MTBE
biodegradation. Results of the experiment demonstrated 1) the
rate of MTBE biodegradation was proportional to the
concentration of dissolved oxygen in water and 2) MTBE uptake
followed a Michaelis-Menten kinetics with respect to dissolved
oxygen.
Special Biochemical
Considerations in the Oxygen-Mediated Biodegradation of MTBE
As additional data sets were
reviewed, an interesting pattern emerged. In many, although
not all cases, it appeared that when MTBE and background
hydrocarbons (typically BTEX) were co-mingled, the BTEX was
preferentially remediated and its concentration had to drop
before significant MTBE degradation could proceed. Prompted by
such field results, a series of laboratory experiments were
conducted to test whether background hydrocarbons interfere
with MTBE degradation. If so this would be a case of classical
competitive inhibition and if proved true would be an
important finding, because it would mean that oxygen
supplementation would have dual value. In other words,
oxygenation could now be used to facilitate the removal of
competing hydrocarbons as well as MTBE itself.
To test the hypothesis, aerobic
bacteria known to be capable of degrading MTBE and BTEX were
isolated with the assistance of Don Phipps at the Orange
County Water District, Fountain Valley, CA. These bacteria
were able to exist on a medium with MTBE as the sole carbon
source. In the experiment, performed by William Farone of APC
in Anaheim, CA, the MTBE degraders were challenged with xylene
as a representative BTEX hydrocarbon (relative to the
chromatographic methods xylene could be handled conveniently
in relation to MTBE on the same column). The results showed
that MTBE degradation was inhibited by xylene; during a seven
day period there was a 52% reduction of MTBE in the absence of
xylene versus a 9% reduction of MTBE with xylene present.
More advanced studies were then
conducted by William Mahaffey of Pelorus EnBiotech in
Evergreen, CO. His work explored the hypothesis that MTBE
biodegradation is 1) an aerobic co-oxidative process and 2)
that competitive inhibition could exist between a primary
substrate and MTBE and 3) that co-oxidation of MTBE may be
limited by the availability of reducing equivalents required
by the initial oxygenase enzyme system. A working hypothesis
was advanced based on structure activity relationships and an
assumption that the most likely primary substrates involved in
co-oxidation and competitive inhibition are compounds found at
the aerobic fringe of a petroleum hydrocarbon plume. Thus
target substrates for co-oxidative metabolism of MTBE were;
methane, alkanes, cycloalkanes, benzene and o-xylene,
Initial studies, using resting cell transformation tests,
demonstrated that substantial removal of MTBE was achieved
with cultures that were acclimated to benzene, camphor, o-xylene
and cyclohexanone (Mahaffey, unpublished). In these early
tests a specific benzene acclimated culture, designated
PEL-B201, was found to be most efficient in degrading MTBE
(58% removal). This established the possibility that a single
enzyme system could metabolize both MTBE and a primary
substrate thus being under the influence of competitive
inhibition dynamics. Support for the competitive inhibition
hypothesis was obtained by demonstrating both MTBE inhibition
of benzene metabolism and the inhibition of MTBE metabolism
with increasing benzene concentrations. Subsequent studies (Koenigsberg
et al , 1999) demonstrated clearly that MTBE inhibits oxygen
uptake associated with benzene metabolism.
Benzene induced cell
suspensions degrade >99% of the added MTBE, while increasing
levels of benzene (1.9 uM and 3.8 uM) resulted in a
significant reduction in the rates of MTBE degradation. No
degradation of MTBE was observed with cells grown on the
non-inducing substrate succinate. The lack of MTBE degradation
on succinate grown cells demonstrated that the MTBE metabolism
occurs with an enzyme system associated with benzene
metabolism and reaffirmed the hypothesis that MTBE is
metabolized by co-oxidation.
Unpublished studies conducted
at Pelorus have indicated that o-xylene degrading pure
cultures will also efficiently degrade MTBE via a co-oxidative
mechanism. Some preliminary results indicate that the most
efficient MTBE co-oxidizing cultures possess what maybe a
novel pathway of o-xylene metabolism. Studies have established
that oxidation of the aromatic nucleus of o-xylene was the
primary mechanism of attack. However, the formation of o-toluic
acid and 2,3-dihydroxy-o-toluic acid suggested that attack of
the methyl group substituent also occurs. Several strains of
o-xylene degrading organisms have been shown to be
simultaneously adapted to degradation of o-phthallic acid. It
is not clear at this time what the ring fission mechanism is
for these organisms, however they are the most active MTBE
degraders. Inspection of space filling molecular models of
MTBE and o-xylene indicate that the MTBE methyl groups can be
aligned in the same plane as the o-methyl groups of o-xylene.
This is allows for speculation that MTBE could bind to the o-xylene
oxygenase active site in a manner that they may align the
methyl groups in the appropriate configuration for oxidative
attack. Studies such as these continue to expand the possible
mechanisms available to microorganisms for the degradation of
MTBE in the environment.
Current Status of Oxygen
–Mediated MTBE Bioremediation
In a second wave of field
activity, several end users of ORC published papers on their
results. These include Boyle et al., (1999), Buzea and
DeStefanis (1999), and Defibaugh and Fishman (1999). In one of
the studies (Buzea and DeStefanis, 1999), BTEX and MTBE
contamination in a fine grained sediment was treated with ORC
through a series of push-point injections.
Since these studies a number of
other major field projects have been executed. Recently,
Patrick Hicks and Michelle Pahr of Arcadis Geraghty and
Miller, in collaboration with J.P. Messier of the U.S. Coast
Guard, performed a full-scale in situ bioremediation of
dissolved phase MTBE and BTEX at a USCG facility in Elizabeth
City, NC. At the facility, three 10,000-gallon fiberglass
underground storage tanks (USTs) had leaked and, after
excavation and removal of the USTs, free phase Jet Fuel (JP-5)
and groundwater were observed in the bottom of the excavation.
Depth to groundwater at the site is approximately 2 m below
land surface (bls). The goal of the project was to enhance the
natural attenuation of dissolved petroleum constituents
without interfering with facility operations.
Aquifer oxygenation was
accomplished by injecting ORC into the contaminated aquifer.
The source area near a former UST was treated with 18
injection points. Each source area injection point received a
slurry suspension of 35 pounds of ORC. The plume portion was
treated with 13 injection points. Each plume area injection
point received a slurry suspension of 22 pounds ORC. A
secondary treatment event in the plume area included 16
injection points. Each injection point received a slurry
suspension of approximately 33 pounds of ORC.
Post treatment monitoring of
the aquifer indicated the dissolved MTBE mass was reduced
100%in both the source and plume areas. The dissolved BTEX
mass was reduced 99% in the source area, and 53% in the plume
area. Site closure has been obtained from the North Carolina
Department of Environment and Natural Resources, Division of
Environmental Management.
With respect to ORC barriers, a
major field research study was conducted by Barcelona and
Jaglowski (1999). In the study, an in-situ reactive tracer
test was conducted at the former Wurtsmith AFB in Oscoda, MI.
An ORC oxygen barrier was constructed and over 11,000
measurements were taken at over 3,500 locations and times
during an 8-month period. The results were marginally positive
with the authors stating that “evidence exists for the
degradation of MTBE through TBA in a highly oxidizing
environment” while also noting that “MTBE has been observed to
degrade under suboxic conditions”. Since there is other
supporting evidence for anaerobic degradation of MTBE,
although the role of aerobes is much less equivocal at this
time, both mechanisms may have been operating in this system.
With respect to the ORC
barrier, it produced a significant level of oxygen (20-30 ppm),
however the groundwater flow rate was fairly high (1.3
ft./day) and this limited residence time in the barrier zone.
Additionally, the experimentally constructed plume, which was
created upgradient and allowed to migrate toward the barrier,
hit the barrier at very low ppb concentrations. Being at the
“tail end of the asymptote” can be problematic with respect to
seeing significant degradation in a short residence time. The
lesson learned was that when barriers are used they would be
more effective in combating higher concentration and/ or lower
flow rate regimes.
Eventually, that opportunity
presented itself through the work of James Landmeyer and his
colleagues at the U.S. Geological Survey Office in Columbia,
SC. The following is a synopsis of the first intensive and
definitively positive ORC barrier study as prepared by
Landmeyer.
“Microbial communities
indigenous to a shallow ground-water system near Beaufort,
South Carolina were observed to degrade milligram per liter
concentrations of methyl tert-butyl ether (MTBE) under natural
and artificial oxic conditions (Landmeyer et al., 2001).
Significant MTBE biodegradation was observed where anoxic,
MTBE-contaminated ground water discharged to a concrete-lined
ditch. In the anoxic ground water adjacent to the ditch,
concentrations of MTBE were greater than 1 mg/L. Where ground
water discharge occurs, dissolved oxygen (DO) concentrations
beneath the ditch exceeded 1.0 mg/L to a depth of 1.5 meters,
and MTBE concentrations decreased to less than 1 µg/L prior to
discharge. MTBE mass flux calculations indicate that 96% of
MTBE mass loss occurs in the relatively small oxic zone prior
to discharge. Samples of a natural microbial biofilm present
in the oxic zone beneath the ditch completely degraded [U-14C]
MTBE to 14C-CO2 in laboratory liquid culture studies, with no
accumulation of intermediate compounds. Upgradient of the
ditch in the anoxic, MTBE and BTEX-contaminated aquifer,
addition of a soluble oxygen release compound resulted in oxic
conditions and rapid MTBE biodegradation by indigenous
microorganisms. In an observation well located closest to the
oxygen addition area, DO concentrations increased from 0.4 to
12 mg/L in less than 60 days and MTBE concentrations decreased
from 20 to 3 mg/L. In the same time period at a downgradient
observation well, DO increased from less than 0.2 to 2 mg/L
and MTBE concentrations decreased from 30 to less than 5
mg/L.”
“This biodegradation of MTBE in
a shallow ground-water system at locations of natural and
artificial oxic conditions is important in light of the large
amount of evidence that exists suggesting that MTBE is
relatively recalcitrant in many ground-water systems, and that
MTBE would therefore preferentially accumulate. Those studies
indicated that the success of bioremediation strategies such
as natural attenuation would likely be low in plumes
containing MTBE, and that remediation could only occur if
contaminated aquifers were inoculated with specific
microorganisms derived from enrichment cultures shown to
degrade MTBE. However, the results of this study demonstrate
that significant natural attenuation of MTBE can occur if the
oxygen limitations naturally associated with gasoline releases
can be removed, either under natural conditions where
discharging anoxic ground water comes into contact with
oxygen, or artificial conditions where oxygen can be added to
aquifers containing mg/L concentrations of MTBE. This final
solution may be an effective strategy for intercepting
characteristically long MTBE plumes, particularly at those
sites not characterized by ground-water discharge to land
surface.”
Conclusion
Presently, there is a
significant and growing body of evidence that oxygen
enrichment of the sub-surface can facilitate the remediation
of MTBE. This paper has documented the first evidence for the
efficacy of field applications of oxygen, in this instance
through the use of a time-release oxygen technology, ORC.
Also, new contributions to understanding basic biochemical
mechanisms of degradation that are oxygen dependent have been
offered. These results were unfolded from a number of extant
commercial data sets, with the support of the fundamental
laboratory studies as cited. In addition to the use of ORC,
others as cited have supported the essential conclusions
through the use of sparged air or oxygen in their field work,
and most recently, there have been two widely recognized,
large-scale studies in this area (Salanitro et al., 1999;
Mackay et al., 1999).
The decision to use of ORC or
sparging to achieve desired objectives involves a basic series
of economic and practical considerations and is beyond the
scope of this paper. While it will be left to the consultant
to sort out the exact needs which are highly case dependent,
the advantages of having a passive, low cost and long term
option for supplemental oxygenation is compelling. ORC
technology seems particularly attractive for plume cut-off
strategies by employing an easily injectable oxygen barrier.
The total installed cost (injection and materials) for a
barrier that is 100 feet in length and 10 feet into the
aquifer is about $10,000 with variable yearly replacement
requirements.
In the broader sense both ORC
and sparging oxygenation technologies have established the
essential fact that MTBE is aerobically biodegradable under
field conditions and that accelerating the natural attenuation
of MTBE by providing supplemental oxygen is a valid and
important engineering objective in site management.
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