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A Smaller Intrusion
by Anthony J. Buonicore, P.E.
May 1, 2009
Reducing the area of concern in the ASTM vapor intrusion standard could make the screening process much more efficient.
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| A former industrial site located near a residential area which caused a vapor intrusion issue. |
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Based upon feedback from the marketplace since the ASTM E
2600-08 vapor intrusion standard was published in March 2008, [1]
the standard is currently undergoing revision. There are two proposed technical
revisions that will enable the area of concern (AOC) for vapor intrusion
screening in real estate transactions to be significantly reduced and save
considerable time.
The first technical revision is directed at
differentiating in Tier 1 between what steps to take when groundwater flow
direction cannot be estimated (in the Phase I investigation) and when it can.
The second revision would eliminate the secondary area of concern (AOC) in Tier
1 as field experience to-date has shown it not to be necessary. Moreover, it
can waste valuable time and money investigating sites a considerable distance
from the target property (TP) that are highly unlikely to result in a vapor
intrusion problem.
Starting with the basics
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| An old waste dump area located near a residential area that created a vapor intrusion issue. |
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These proposed revisions in the standard have the potential
to significantly reduce the AOC, and thus the time and cost of investigations.
The existing standard identifies a primary and secondary AOC in the Tier 1
search distance test, distinguished by whether the record search is done within
the area completely around a target property (primary AOC), or whether the
up-gradient direction beyond the primary AOC (secondary AOC) is included as
well.
Also, the search distances are different for sites
contaminated with volatile and semi-volatile chemicals of concern (COC) – such
as many chlorinated solvents – versus sites contaminated with petroleum
hydrocarbon COC – such as BTEX. The search distances are shorter for petroleum
hydrocarbons because they are known to undergo significant bio-degradation in
the presence of oxygen. The primary AOC search distances were determined based
upon conservative consideration of both plume length and the distance vapors
might travel along a path of least resistance from a source (such as
contaminated groundwater) through the vadose zone directly to a structure on a
TP. The secondary AOC was included to keep the search distances in the E
2600-08 standard consistent with those in the E 1527-05 Phase I standard. [2]
There is sound technical basis for establishing the primary
AOC. Plume length research was conducted for both volatile chemical plumes
(such as chlorinated solvent plumes from dry cleaners) and volatile petroleum
hydrocarbon plumes from leaking underground storage tank sites. In order to be
conservative, the plume length selected to determine the primary AOC was based
upon the 90th percentile distance. [3-6] For (non-petroleum
hydrocarbon) COC plumes – such as may be associated with dry cleaners – 90
percent of the time the plume length was less than approximately 1,590 feet.
For volatile petroleum hydrocarbon COC plumes, 90 percent of the time it was
less than approximately 390 feet.
Using experience from vapor intrusion sites in the U.S. on
the distances vapors may migrate through the vadose zone, and adding them to
the 90th percentile plume length, the primary AOC search radii were determined,
i.e., 1/3 mile (1,760 feet) for non-petroleum hydrocarbon COC, and 1/10 mile
(520 feet) for petroleum hydrocarbon COC.
Under the proposed technical revisions, if it is
not possible to estimate groundwater flow direction in the Phase I
investigation, then the Tier 1 screen must consider all known or suspect
COC-contaminated property surrounding the TP within the search radii of the
primary AOC, as defined in the existing standard. However, if it is possible to
estimate groundwater flow direction (and assuming four quadrants can be distinguished
around a TP: an up-gradient, two cross-gradient, and a down-gradient), then the
AOC can be further reduced. This is important because each known or suspect
contaminated property within the AOC may need to be investigated further, and
may even require a file review at state regulatory offices (in accordance with
Tier 2 of the standard). The key consideration is where the known or suspected
contaminated property is located with respect to the TP.
Contaminated sources located up-gradient of the TP
For
contaminated sources – such as a drycleaner with a PERC release or a gas
station with a release from a leaking underground storage tank – located
up-gradient of the TP, the focus would continue to be those contaminated
properties within the primary AOC distances (i.e., 1,760 feet for COC sources
and 520 feet for petroleum hydrocarbon COC sources).
For contaminated sources located cross-gradient of the TP
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| A former gas station site. |
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When a contaminated property (such as a drycleaner with a
PERC release or a gas station with a release from a leaking underground storage
tank) is located cross gradient from the TP, the length of the plume associated
with the cross-gradient source is not really relevant. However, its width is
relevant. According to the E 2600-08 standard, what matters for cross-gradient
sources is whether the nearest edge of the contaminated plume is within the
critical distance from the nearest structure on the TP. The critical distance
as defined in E 2600-08 effectively is the maximum distance a vapor can
reasonably be expected to migrate in relatively permeable soil, assuming the
path of least resistance is directly from the nearest edge of the contaminated
media (such as groundwater) to the nearest structure on the TP. The distance of
concern from the structure on the TP to the property that created the
contamination (e.g., a dry cleaner), would be the critical distance plus a
distance to account for the plume width at that point. While the critical
distance numbers are specifically identified in E 2600-08 for petroleum
hydrocarbon and non-petroleum hydrocarbon contamination, nothing prescriptive
is mentioned in the standard about how to deal with plume width if such
information is not available. A suggested approach is described later.
For contaminant sources located down-gradient of the TP
For
contaminated sites – such as a dry cleaner with a PERC release or a gas station
with a release from a leaking underground storage tank – located down-gradient
of the TP, plume length and width matter little and the focus would only be on
the critical distance. Hence, the AOC can be reduced from 1,760 feet to 100
feet for COC contamination, except for petroleum hydrocarbon COC contamination
where the AOC can be reduced from 520 feet to either 100 feet (when LNAPL or
free product is presumed to be present), or 30 feet (when only dissolved
petroleum hydrocarbons are presumed to be present in the groundwater).
Suggested methodology for dealing with plume width at cross-gradient sources
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| A former drycleaners. Such sites present high potential risk in any vapor intrusion screen. |
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For contaminated properties located cross-gradient from the
TP, plume width must be taken into consideration in selecting an appropriate
distance of concern (D concern). The question is, what
would be a reasonably conservative estimate for plume width (a default value)
to use in the screening process assuming no actual plume information is
available?
One approach is to base the default plume width on 1/3rd of
the plume length [7,8] and, to be conservative, use the
90th percentile plume length (PL90) discussed previously, regardless of where
the contaminated property is located in the cross-gradient quadrant. Plume
width, for example, would matter little if the contaminated property is located
close to the boundary separating the cross-gradient quadrant from the
down-gradient quadrant. On the other hand, it would be of much greater concern
if the contaminated property is located close to the boundary separating the
cross-gradient quadrant from the up-gradient quadrant.
Assuming symmetry of the plume on both sides of the source,
one-half of the plume width (PW) would be added to the critical distance (D critical)
to establish the distance of concern. This can be expressed as:
Dconcern = Dcritical
+ 1/2 PW = Dcritical + 1/2 (PL90/3)
Comparing this approach for default plume width with actual
plume data [3-6] suggests the approach is reasonable. For
non-petroleum hydrocarbon COC contamination sources (such as a dry cleaner)
located cross-gradient from the TP:
Dcritical = 100 ft.
PL90 = 1,590 ft.
Therefore:
Dconcern = 100 + 1/2 (1,590/3) = 365
feet
The default E 2600-08 search radius in the cross-gradient
quadrant can then be reduced from 1,760 feet to 365 feet for non-petroleum
hydrocarbon COC.
For LNAPL or free product petroleum hydrocarbon sources
(such as a gas station with a release from a leaking underground storage tank)
located cross gradient from the TP:
Dcritical = 100 ft.
PL90 = 390 ft.
Therefore:
Dconcern = 100 + 1/2 (390/3) = 165
ft.
Using this approach, the default E 2600-08 search radius in
the cross-gradient quadrant could then be reduced from 520 feet to 165 feet for
LNAPL petroleum hydrocarbon sources. If only dissolved petroleum hydrocarbons
(in groundwater) are presumed to be present:
Dcritical = 30 ft.
PL90 = 390 ft.
Therefore:
Dconcern = 30 + 1/2 (390/3) = 95 ft.
Using this approach, the default E 2600-08
search radius in the cross-gradient quadrant could then be reduced from 520
feet to 95 feet for dissolved petroleum hydrocarbon sources.
Status of E 2600-08
Several changes are planned for the ASTM E 2600-08 standard
that should improve its practicality, clarity and consistency. These changes
were balloted in April 2009. After discussion of these changes and any further
revisions, there will be another ballot in summer 2009. If all goes well, it is
anticipated that the revised standard could be approved at the October 2009
ASTM meeting in Atlanta and published by the end of the year.
Furthermore, using reasonable assumptions, it
may be possible to reduce significantly the default distances of concern, which
could significantly reduce the investigation effort in many cases with minimal
reduction to the protectiveness of the screening process. PE
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Anthony J. Buonicore, P.E. ajb@edrnet.com
Anthony Buonicore is a consultant and chaired the ASTM task
group responsible for developing the vapor intrusion assessment standard. He
can be reached at (800) 238-1841, or ajb@edrnet.com.
References 2. ASTM Standard Practice E 1527-05 for Environmental Site Assessments: Phase I Environmental Site Assessment Process, published by ASTM, West Conshohocken, PA, November 1, 2005.. 1. ASTM Standard Practice E 2600-08 for Assessment of Vapor Intrusion into Structures on property Involved in Real Estate Transactions, published by ASTM, West Conshohocken, PA, March 3, 2008.. 5. State Coalition for Remediation of Dry Cleaners, www.drycleancoalition.org.. 3. American Petroleum Institute, Bulletin No. 8, Characteristics of Dissolved Petroleum Hydrocarbon Plumes: Results from Four Studies, Newell, C.J. and Connor, J.A., December 1998.. 4. Newell, C.J., Hopkins, L.P. and Bedient, P.B., A Hydrogeological Database for Ground-Water Monitoring, Ground Water, Vol. 28, No. 5, 703-714, September/October 1990.. 8. Domenico, P.A., An Analytical Model for Multidimensional Transport of a Decaying Contaminant Species, J. Hydrology, Vol. 91, 49-58, 1987.. 7. Gelhar, L.W., Welty, C. and Rehfeldt, K.R., A Critical Review of Data on Field-Scale Dispersion in Aquifers, Water Resources Research, Vol. 28, No. 7, 1955-1974, 1992.. 6. Mace, R.E., Fisher, R.S., Welch, D.M. and Parra, S.P., Extent, Mass and Duration of Hydrocarbon Plumes from Leaking Petroleum Storage Tank Sites in Texas, Geological Circular 97-1, Bureau of Economic Geology, University of Texas at Austin, 1997..
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