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By Michael J.
Day
Applied Hydrology Associates,
Inc., Denver, Colo.
mday@appliedhydrology.com
Abstract
Fuel leaks
from underground storage tanks (USTs) and piping have been a
major source of groundwater contamination. In the US and
Europe, regulations requiring upgrading of USTs to meet
specific standards have significantly reduced instances of
fuel contamination. However, complete containment of tank and
piping systems is generally not required, and routine
groundwater monitoring is not usually performed. The
limitations of UST leak detection systems result in a
situation where contamination of groundwater by fuel
components may occur due to undetected leaks from uncontained
UST systems. The fate and transport characteristics of fuel
components significantly influence the potential risk to
groundwater supplies and the methodologies to manage and
remediate contamination resulting from UST leaks. The
recognition that oxygenates in fuels tend to be more mobile in
groundwater systems has put an increased emphasis on early
detection and response to fuel leaks and spills.
Introduction
Leaks of fuel
from underground tanks and associated piping have been a major
source of groundwater contamination. The fate and transport
characteristics of fuel components significantly influence the
potential risk to groundwater supplies and the methodologies
to manage and remediate contamination resulting from UST
leaks. Understanding the fate and transport of fuel
components under various hydrogeologic and geochemical
conditions is critical to developing an appropriate management
plan. The recognition that oxygenates in fuels tend to be
more mobile in groundwater systems has put an increased
emphasis on early detection and response to fuel leaks and
spills.
Phase Transformation of Fuel
Components
Fuel
components may be converted from the fuel liquid phase to the
air, water, and solid-phases by a variety of physical,
chemical, and biological processes that can occur in the
subsurface. The physical and chemical characteristics of
organic compounds tend to govern the tendency for the compound
to favor certain phases over others. For example, highly
soluble compounds will favor the water phase over the air or
solid phases.
The
volatilization process from the liquid phase to the vapor
phase is driven by concentration gradients. Given sufficient
time, in a closed system, equilibrium will be established
between concentrations of a compound in the air and in the
released fuel. The vapor pressure of a volatile fuel
component, which is temperature dependent, is a measure of the
tendency of that component to move from the liquid to the
vapor phase. The more volatile constituents of fuel will tend
to be most readily vaporized. The partial pressure of a
volatile component in equilibrium with fuel is equal to its
pure-phase vapor pressure multiplied by its fractional content
in the fuel as described by Raoult’s Law (Barker and others,
1991). Therefore, as a volatile component in the NAPL is
reduced, both the contact efficiency and the partial vapor
pressure is also reduced, making it more difficult for the
component to volatilize.
The
partial pressure of MTBE is higher than other fuel components
and it will therefore volatilize more readily.
Volatilization and condensation are complementary processes
that describe the exchange of a volatile compound between
water and air. Volatilization refers to the movement of the
compound from water into air whereas condensation refers to
the movement from air into water. The interchange between the
soil vapor and the pore water will occur within the vadose
zone and at the water table interface. Equilibrium can be
established between concentrations of a compound in air and
water as described by the Henry's Law constant, which is
temperature dependent. If the same units are selected for the
air and water concentrations, then the Henry's Law constant is
dimensionless. A compound with a value of 0.05 or larger is
considered to volatilize easily from water. In comparison
with BTEX components, ethanol and MTBE both tend to partition
strongly from the gas phase into the water phase.
Consequently, dissolved ethanol and MTBE tend to stay in the
water phase.
Solution
describes the process of component exchange from the fuel
phase into the water phase. Solution of fuel components will
occur within the pore water of the vadose zone as well as in
the saturated groundwater zone below the water table.
Infiltrating water that passes through soils affected by fuel
leaks will tend to dissolve the volatile components of
residual fuel within the soils. Water solubility is probably
the most important chemical property affecting the
partitioning of organic compounds between fuel and water.
Ethanol is infinitely soluble in water and MTBE is more
water-soluble than the BTEX compounds in fuels. The
pure-phase solubility of an organic compound in fuel is
reduced in proportion to its fractional content in the fuel
because of partitioning between the organic mixture and water
(Barker and others, 1991). For example, a reformulated
gasoline that is 10% by weight MTBE and 1% benzene, reduces
the solubility of MTBE in water to about 4,300 mg/L and
benzene to about 18 mg/L. In contrast, for a nonoxygenated
gasoline, the total hydrocarbon solubility in water is
typically about 120 mg/L (Poulsen and others, 1992). Because
of their relatively high concentration in reformulated
gasoline and their water solubilities, oxygenates such as
ethanol and MTBE will tend to be found in higher
concentrations than BTEX in shallow groundwater that is in
contact with oxygenated gasoline released from UST leaks.
Water
solubility also affects the partitioning of organic compounds
between water and subsurface solids. Many organic compounds
exhibit water solubilities in the low milligrams-per-liter to
micrograms-per-liter range. In general, these low
solubilities indicate a strong partitioning to the organic
carbon associated with the subsurface solids. The relatively
high solubilities of ethanol and MTBE result in a tendency for
these constituents to stay in the water phase and not sorb to
subsurface solids. The tendency for compounds to sorb to the
organic phase of soils is also reflected by the organic
partition coefficient (Koc). Ethanol and MTBE have
low Koc values in comparison to BTEX components,
reflecting their lesser affinity for soil adsorption.
Degradation
of an organic compound refers to its transformation by abiotic
or biotic reactions. Other organic compounds may be formed as
byproducts of the degradation process. Complete degradation
(mineralization) of an organic compound to carbon dioxide and
water is almost always associated with some form of microbial
activity. Biological transformations can involve many
reactions and may require a long period of time to complete,
but often provide the predominant decay pathways in water and
soil.
It is well
documented that BTEX compounds undergo biological
transformations in groundwater. Ethanol is readily
biodegradable under aerobic and anaerobic conditions (Powers
et al, 2001). There is increasing evidence that MTBE also
naturally degrades, particularly under aerobic (oxygenated)
conditions, albeit at a rate generally slower than the BTEX
compounds, and under methanogenic conditions (Wilson et al,
2000). This indicates that some indigenous microorganisms are
able to degrade MTBE (Thomas and others, 1988). Ongoing
research projects, such as at Vandenberg AFB in California,
have demonstrated that adding oxygen may be extremely
effective in stimulating indigenous biodegradation of MTBE
(McKay, 2000).
Biodegradation in the vapor phase can also occur, particularly
if atmospheric exchange allows the continued introduction of
oxygen to promote aerobic respiration. Barometric and
temperature variations associated with diurnal fluctuations
and storm events can produce air exchanges between the
atmosphere and the soil vapor of the vadose zone (Massmann and
Farrier, 1992). Vapor phase biodegradation of organic
compounds is usually much faster than aqueous phase
biodegradation as long as there is sufficient water vapor
present.
Fate and Transport Processes at
LUST Sites
Fate and
transport of fuel components in the subsurface at leaking
underground storage tank (LUST) sites are determined by their
physical and chemical characteristics and by the hydrogeologic
and geochemical conditions at the site. A leak in one or more
tanks at an LUST site may provide a source of fuel to the
subsurface. As long as the source of the fuel release
continues, the subsurface extent of fuel liquid will continue
to expand until it reaches a physical barrier (such as the
water table), or until natural processes remove the fuel
components at the same rate as they are introduced.
The fate
and transport of fuel components released from a typical LUST
site are discussed in terms of three distinct zones where
different hydrogeological conditions exist. The zones
considered are: (a) the tank backfill, (b) the unsaturated or
“vadose” zone below the tank backfill and above the
groundwater table where the soil pores are not entirely
saturated with water, and (c) the saturated groundwater within
a shallow unconfined aquifer below the LUST site.
Tank
Backfill Zone
Typically,
a fuel retail station has several USTs located in a common
excavation that is backfilled with clean sand. The depth to
the base of the tank backfill is usually 8 to 10 feet (2.5 to
3 meters) below ground surface, depending on the size of the
USTs. The sandy backfill materials would be expected to have
fairly high permeability. The excavated area is usually
capped with asphalt so that infiltration of surface water into
the tank backfill is very limited. Typically, the tank
excavation is not lined prior to tank installation and sand
backfilling, so that there is direct hydraulic connection
between the backfill and the native soils. In areas where the
natural groundwater table is close to the ground surface, the
base of the underground tanks may be in water-saturated
backfill. More typically the tank backfill is located well
above the natural groundwater table and the backfill sands are
unsaturated.
In the case
of a LUST in an unsaturated backfill, released fuel will tend
to migrate by gravity to the base of the tank backfill. If
the native soils are less permeable than the tank backfill,
fuel will tend to accumulate and spread out at the base of the
backfill. If the tank “pit” is unlined then fuel will
eventually accumulate in the backfill to the point where it
will overcome the air-entry pressure of the underlying soil
pores and start to infiltrate into these soils.
The major
processes operating in the tank backfill are migration of the
non-aqueous phase liquid (NAPL) fuel and volatilization of
released fuel into the air within the backfill pore spaces.
Soil vapor transport of fuel constituents can occur through
diffusion and advection processes in the tank backfill.
Biodegradation in the vapor phase can also occur, particularly
if atmospheric exchange allows the continued introduction of
oxygen to promote aerobic respiration.
In cases
where the tanks are located well above the natural groundwater
table, the backfill provides an aerated zone that can be
monitored for fuel vapors as a method of leak detection. MTBE
has the highest vapor pressure of all the volatile
constituents within oxygenated fuels. It also may constituent
a relatively high percentage of the fuel (10 to 15% in
reformulated and oxyfuels) and so will tend to be found in the
highest concentrations in soil vapor. Due to its high vapor
pressure, monitoring of fuel vapors is a particularly
effective method for detection of MTBE. Low-volume soil vapor
venting of tank and piping backfill can also be used to detect
and remove the volatile components of fuel from small chronic
leaks (Day et al, 2001).
Vadose
Zone
If the tank
pit is unlined, accumulation of fuel in the tank backfill will
eventually lead to infiltration of the underlying soils of the
vadose zone. Fuel would continue to migrate both vertically
and laterally at a rate determined primarily by the
stratification and permeability of the native soil materials.
Stratification of the native soils in the vadose zone beneath
the tank backfill will tend to cause localized accumulation
and lateral migration of fuel. If the fuel reaches the water
table, it will tend to “float” and spread out on top of the
saturated water zone due to its lower density.
The major
processes that occur within the vadose zone are
volatilization, condensation, solution, adsorption, and
biodegradation. Volatilization of released fuel will continue
to occur into the air-filled pore spaces of the vadose zone.
Soil moisture in the vadose zone will interact with soil vapor
and allow exchange of volatile fuel constituents from the air
phase to the water phase.
Once the
fuel components are in the air or water phase they can
continue to migrate under the prevailing geologic conditions.
Soil vapor transport of fuel constituents can occur through
diffusion and advection processes in the soil vadose zone.
Mass loss of fuel components to the atmosphere can occur at
the land surface interface if the constituent remains in the
vapor phase. In arid and semiarid environments, the vadose
zone will have a relatively low moisture content over most of
the year and there is limited opportunity for fuel
constituents that have volatilized directly from leaked fuels
to solubilize into the water phase as a result of vapor
contact with soil moisture. However, if the soil moisture
content in the vadose zone is high, then relatively soluble
compounds such as ethanol and MTBE will not tend to stay in
the vapor phase.
The overall
downward velocity and travel times of infiltrating water
containing dissolved gasoline constituents originating at a
LUST site depends on many factors, such as recharge rate,
horizontal and vertical hydraulic conductivity of the
materials in the vadose zone, and the thickness of the vadose
zone. However, due to the different physical characteristics
of the gasoline components, they tend to migrate in the
dissolved phase at different rates. Migration of dissolved
ethanol and MTBE in the vadose zone does not tend to be
retarded by sorption to soils and it therefore moves to the
ground water at almost the same velocity as the recharge
water. The dissolved BTEX components of gasoline will tend to
migrate at a slower rate due to their higher tendency to be
sorbed to the soils.
Aerobic
biodegradation of all dissolved constituents that may occur
within the vadose zone will reduce the overall mass of
constituents reaching the groundwater table. The more mobile
constituents of oxygenated fuels, such as ethanol and MTBE,
will tend to be at the leading edge of an advancing dissolved
“front” and therefore have the most exposure to soil air (and
oxygen) in the vadose zone. Aerobic degradation tends to be
most active at the front and edges of the dissolved plume of
fuel constituents where oxygen contents are highest, so that
ethanol and MTBE have the highest potential for degradation.
Consumption of oxygen by biological degradation processes can
lead to anaerobic conditions behind the leading edge of the
dissolved plume so that degradation of less mobile dissolved
constituents is not as rapid. Several researchers have
speculated that the high biodegradability of ethanol could
lead to increased mobility of BTEX constituents within a
depleted oxygen “shadow” behind an advancing ethanol front
(Powers et al, 2001).
Saturated
Aquifer Zone
If leakage
of fuel is sufficient, it may eventually migrate to the water
table, where it will tend to “float” and spread out on top of
the saturated water zone due to its lower density. The
accumulation of fuel at the water table will provide a source
for dissolved constituents in the saturated groundwater zone
below the water table. The major processes that occur within
the saturated zone are dissolution, advection, dilution,
dispersion, adsorption, diffusion, and biodegradation.
Volatilization of dissolved fuel constituents can also
continue to occur at the air-water interface if the saturated
groundwater is unconfined.
Constituents from released fuels that dissolve into
groundwater will migrate at a rate dependent on their tendency
to sorb onto the soil matrix. The ratio of the groundwater
velocity to the velocity at which a compound is transported is
frequently referred to as the retardation factor, R. The
actual values of R for a particular compound depend on the
organic partition coefficient (Koc) of the compound
and aquifer properties, such as porosity, bulk density, and
organic carbon content. A compound that moves at one-half the
velocity of the ground water has an R value of 2. Once
ethanol or MTBE is in the saturated zone groundwater, their
low adsorption characteristics allow them to move at virtually
the same velocity as the groundwater (i.e. their R values are
fairly close to 1 for typical aquifers). BTEX compounds have
R values that can range from 1.1 to about 2.0 (Zogorski and
others, 1997). Ground-water flow velocities vary widely
depending on several factors including the permeability,
porosity, and hydraulic gradient of the aquifer. Velocities
under typical hydraulic gradients can range from a few
millimeters per year to a meter per day. Ground-water
velocities near a pumping well tend to be higher due to
increased hydraulic gradients existing near these wells.
Dispersion
will tend to mix and dilute the concentrations of fuel
constituents within the saturated groundwater zone.
Dispersion will tend to be more apparent in more heterogeneous
aquifer systems. Dilution of dissolved constituents by mixing
with unaffected groundwater recharge is also commonly observed
in unconfined aquifers. Recharge that occurs along the flow
path of an affected groundwater plume will tend to establish a
downward vertical hydraulic gradient and cause the affected
groundwater plume to migrate downwards. This has been
referred to as a “sinking” plume, and is most apparent in
situations where an affected groundwater plume has migrated
over a significant lateral distance.
Diffusion
of dissolved constituents into lower permeability lenses
within the aquifer, or confining units above and below the
aquifer, may also contribute to a decrease in constituent
mass. Diffusion effects will be most apparent in highly
stratified aquifer units.
Due to their
chemical characteristics, oxygenates such as ethanol and MTBE
tend to be more mobile in groundwater than other fuel
components. Ethanol would be expected to degrade very quickly
in the subsurface so that it would not tend to persist.
However, very few field studies of ethanol in groundwater have
been performed so that this assumption has not been verified.
The high biodegradability of ethanol could lead to increased
mobility of BTEX constituents due to a decreased rate of
biodegradation of these constituents within a depleted oxygen
“shadow” behind an advancing ethanol front (Powers et al,
2001).
The detection
of MTBE ahead of benzene in downgradient monitoring wells at
many LUST sites would tend to support the expected higher
mobility of MTBE. However, several field studies have not
shown a significant difference in MTBE and benzene plume
lengths, suggesting that natural attenuation processes for
MTBE have typically been underestimated. Where MTBE plumes in
groundwater persist or grow, this can usually be attributed to
a continuing source, including residual fuel in soils below
LUST sites. This emphasizes the importance of early detection
and complete source removal when dealing with releases of
oxygenated fuels.
Implications with Respect to
Managing UST Sites
In the US and
Europe, regulations requiring upgrading of underground storage
tanks (USTs) to meet specific standards have significantly
reduced instances of fuel contamination. Leak detection
systems at gasoline retail stations are primarily dependent on
physical leak measurement systems rather than on indirect
monitoring of backfill or shallow groundwater. These systems
are generally capable of detecting leaks as small as 0.05
gallons (0.2 liters) per hour. Fuel leaks that are smaller
than this detection threshold may remain undetected for long
periods of time and result in releases of fuel to the
subsurface. Federal regulations in the US governing upgraded
USTs do not include the requirement for containment of tank
and piping systems, or for routine groundwater monitoring.
This situation may lead to contamination of groundwater by
fuel components due to undetected leaks from uncontained UST
systems.
Most fuel
components have relatively low solubility, sorb to the soils,
and can be shown to naturally degrade in the subsurface. As a
consequence, natural attenuation processes largely prevent
widespread fuel contamination from leaking USTs. However,
small leaks from USTs might result in gradual groundwater
contamination unless the leaks are detected and appropriate
response taken in a timely fashion.
Due to the
physical and chemical characteristics of fuel oxygenates such
as MTBE, it is clear that the key to managing oxygenated fuels
is to be able to detect releases soon after they occur, and to
respond rapidly with appropriate corrective action.
Undetected releases of fuel from leaking USTs have the
potential to impact shallow groundwater, particularly if
subsurface conditions are not conducive to natural attenuation
processes, and secondary containment does not exist.
Monitoring of the tank and piping backfill for persistent fuel
vapor concentrations under very low vapor extraction
conditions may be the most definitive way to detect small
chronic fuel leaks. For underground tank systems that are
above the groundwater table, this technique is particularly
applicable for MTBE because of its high vapor pressure
characteristic. Venting systems can be installed in existing
tank systems without the necessity of pulling the tanks. This
is a relatively low cost method of preventing groundwater
contamination by volatile fuel components from small chronic
leaks. Routine monitoring of shallow groundwater should be a
component of a leak detection program, particularly in
high-risk areas.
References
Barker, J.F.,
Gillham, R.W., Lemon, L., Mayfield, C.I., Poulsen, M., and E.
A. Sudicky, 1991, Chemical fate and impact of oxygenates in
groundwater--Solubility of BTEX from gasoline--Oxygenate
Compounds: Washington, D.C., American Petroleum
Institute Publication 4531, 90p.
Day, M.J., R.
Reinke, and J.A.M. Thomson, 2001, Fate and Transport of
Fuel Components below Slightly Leaking Underground Storage
Tanks. International Journal of Environmental
Forensics, 3(1), March 2001.
Mackay, D, M.
D. Einarson, R. D. Wilson, B. Fowler, K. Scow, M. Hyman, C.
Naas, M. Schirmer, and G. C. Durrant, 1999, Field Studies
of In-Situ Remediation of an MTBE Plume at Site 60, Vandenberg
Air Force Base, California. Proceedings of the 1999
Petroleum Hydrocarbons and Organic Chemicals in Ground Water:
Prevention, Detection, and Remediation. Houston, TX, Nov.
17-19, 1999, 178-188.
Massmann,
J., and D.F. Farrier, 1992, Effects of atmospheric
pressures on gas transport in the vadose zone. Water
Resources Research, 28(3), 777-791.
Poulsen,
Mette, Lemon, Lloyd, and Barker, J.F., 1992, Dissolution of
monoaromatic hydrocarbons into groundwater from
gasoline-oxygenate mixtures: Environmental Science &
Technology, v. 26, no. 12, p. 2483-2489.
Powers, S.E.,
D. Rice, B. Dooher, P. Alvarez, 2001, Will Ethanol-Blended
Gasoline Affect Groundwater Quality? Environmental
Science & Technology, v. 35, no. 1, p. 24A-30A.
Squillace,
P.J., J.F. Pankow, N.E. Korte, and J.S. Zogorski, 1998,
Environmental Behavior and Fate of Methyl tert-Butyl Ether (MTBE).
U.S.
Department of the Interior - U.S. Geological Survey, National
Water Quality Assessment Program (NAWQA),
Fact Sheet FS-203-96.
Thomas, J.M.,
Clark, G.L., Tomson, M.B., Bedient, P.B., Rifai, H.S., and C.
H. Ward, 1988, Environmental fate and attenuation of
gasoline components in the subsurface: Washington,
D.C., American Petroleum Institute, final report, p. 111.
Wilson, J.T.,
J.S. Cho, B.H. Wilson, and J.A. Vardy, 2000, Natural
Attenuation of MTBE in the Subsurface under Methanogenic
Conditions; National Risk Management Research
Laboratory,
Ada, OK. EPA/600/R-00/006,
49p.
Zogorski,
J.S., and others, 1997, Fuel oxygenates and water quality,
in Interagency Assessment of Oxygenated Fuels:
Washington D.C., Office of
Science and Technology Policy, Executive Office of the
President,
chap. 2, 80 p.
Table 1: Comparison of Fate
and Transport Properties for Fuel Constituents
|
Property |
Unit |
MTBE |
Benzene |
Toluene |
Ethyl-benzene |
Xylene |
Ethanol |
|
Vol % in Gasoline |
Vol % |
10 to 15 |
1 |
5 |
<1 |
8 |
10 |
Molecular Weight1
|
g/mol |
88 |
76 |
92 |
106 |
318.5 |
46 |
|
Specific Gravity1 |
Dimension-
less |
0.74 |
0.88 |
0.87 |
0.87 |
0.86 |
0.79 |
|
Vapor Pressure**2 |
mm Hg |
251 |
95 |
28 |
9 |
8 |
50 |
Partial Pressure
(gasoline)*
|
mm Hg |
25 |
1 |
1.4 |
<0.1 |
0.6 |
5 |
|
Henry’s Law
Constant**2
|
Dimension-
less |
0.02 |
0.22 |
0.24 |
0.35 |
0.31 |
0.00025 |
Log Koc (Adsorption)
2
|
Dimension-
less |
1.05 |
1.9 |
2.0 |
2.5 |
2.6 |
0.7 |
Water Solubility (pure)**
2
|
mg/L |
43,000 |
1,780 |
535 |
161 |
146 |
Miscible |
Water Solubility (gasoline)*
|
mg/L |
4,300 |
18 |
27 |
<2 |
12 |
Miscible |
Odor Threshold1
|
ppbv |
95 |
1,500-4,700 |
160 |
6,000 |
20,000 |
49,000 |
Taste Threshold
|
mg/L |
10-130 |
500-4,500 |
NA |
NA |
NA |
NA |
Biodegradation Rate
|
% per day |
0.01 – 0.1 |
0.1 – 1.0 |
0.1 – 1.0 |
0.1 – 1.0 |
0.1 – 1.0 |
0.33 |
*
Based on gasoline containing 10% mtbe or ethanol, 5%
toluene, 8% xylenes, 1% ethylbenzene, and 1% benzene
**
At a temperature of 25oC
NA
Not Available
1
Urie Environmental, Chemical Substance Hazard
Assessment & Protection Guide, 1994.
2
Fuel Oxygenates and Water Quality: Current
Understanding of Sources, Occurrence in Natural Waters,
Environmental Behavior, Fate, and Significance. Chapter 2 in
Interagency Assessment of Oxygenated Fuel, Office of
Science & Technology Policy, Executive Office of the
President, Washington, D.C., Zogorski, J.S., A. Morduchowitz,
A.L. Baehr, B.J.Bauman, D.L. Conrad, R.T. Drew, N.E. Korte, W.
W. Lapham, J. F. Pankow, and E.R Washington., 1997
3
Malcolm Pirnie, Inc., 1998, Evaluation of the
fate and transport of ethanol in the environment: Report
prepared for the American Methanol Institute, November 1998.
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