The purpose of this memorandum is to further clarify and explain the design changes that warranted the June 22, 1999, Action Memorandum (Attachment 1) that approved an emergency exemption to both the 12-month statutory time limit and the $2 million funding limit for the time critical removal action at the Illinois Central Spring (ICS) Site. This memorandum serves to further memorialize the decision making process of U.S. EPA regarding this removal action and to provide an expanded explanation of the facts that U.S. EPA relied on in determining the need for the June 22, 1999, Action Memorandum in light of comments received after the of that Action Memorandum. This memorandum also provides an update of the status of the design and construction of components of this removal action. The original Action Memorandum was signed by William E. Muno, Director, Superfund Division, on September 30, 1998.
The June 22, 1999, Action Memorandum (providing both the exemption and the added funding) allows for the completion and operation of a 1,000 g.p.m. (gallon per minute) water treatment plant that will effectively remove PCBs from the spring water originating from the contamination source at the Lemon Lane Landfill and outcropping at the spring. As explained in both the September 30, 1998, and June 22, 1999, action memoranda, the Illinois Central Spring water treatment plant is intended to address PCB releases from the Spring during storm events when the water is at its highest flows. The logic for designing and constructing a plant capable of addressing high flow storm water events is that it is during those events that high PCB-mass concentrations are released from the Lemon Lane system and found in the water emerging at the Spring.1 This is in contrast to the substantially lower PCB-mass concentrations found during the more-typical low flow periods. Designing a plant to treat spring water only during low-flow periods would, however, allow releases of extraordinarily large amounts of PCBs to be released into the environment during high-flow storm events.
The funding increase of $3,889,670 brings the project total to $5,998,973. The construction of the plant required by the removal action will be completed by May of 2000. The June 22, 1999, Action Memorandum also allows for up to a year of developing the operational and maintenance requirements at the plant by putting the plant through various staged and real operational scenarios. Thus, U.S. EPA can turn the plant over to the State of Indiana in an operational status for Indiana to operate and maintain as per agreement.
The ICS Site is not on the National Priorities List (NPL), but
the adjacent Lemon Lane Landfill was placed on the NPL in
September 1983. The releases addressed by this removal action
are the result of PCB released from the Lemon Lane Landfill.
The ICS site lies at a Latitude of 39 degrees, 10 minutes, 1.8
seconds North and a Longitude of 86 degrees 33 minutes, 14.9
seconds West.
Please refer to the original Action Memorandum (Attachment 1) and
the June 22, 1999, Action Memorandum for additional information.1
After the signing of the Action Memorandum on September 30, 1998,
work concentrated on the various aspects of a comprehensive
engineering and design by the ERS (Emergency Response Services)
contractor, (Earth Tech). This work included the following:
- A geophysical survey.
- Clearing and grubbing of the 2.1 acre site by a
qualified disadvantaged business.
- Removing the rail and ties from an abandoned railroad
bed. The cleared railroad bed serves as the access
road to the site.
- Further delineation, by sampling, of the "hot" zones
both north and south of the active railroad tracks that
bisect the site.
- Obtaining access agreements on various parcels of
property that affect the site itself and other
necessary activities on adjacent properties.
- Surveying and staking property lines.
- Establishing relationships with City and State
officials, and property owners.
- Establishing a design team of qualified engineers in
many disciplines.
vCompletion of the final design and cost analysis for
the 1,000 g.p.m. water treatment plant. The treatment
plant is designed with flexibility and can be scaled to
address water treatment as a component of the Lemon
Lane remedial action with minimal added costs and with
no break in the operation of the plant.
- A detailed estimate of the operational costs associated
with the plant for a one-year "shake-down" period.
After the issuance of the June 22, 1999, Action Memorandum, the
full scale construction of the ICS water treatment system began.
To date, the following additional tasks have been completed, or
are underway.
- An all weather access road into the plant site and into
the site was built.
- A construction office and a "lay down" yard are
completed.
- Both a temporary fence around the "lay down" yard and a
permanent fence around the treatment system area are
erected.
- The site has been leveled (a cut and fill).
- Permanent power runs into the site.
- Two "jack and bores" under the adjacent Indiana Central
Railroad tracks to the site of the spring have been
completed to assist in storm water diversion.
- Blasting & excavation of the rock where the spring
receiving sump will be located has been completed.
- Construction of the spring receiving sump building is
complete.
- Construction of the treatment plant is 90% complete.
- The yard and utility piping is complete.
- All concrete work in and around the plant is complete.
This includes concrete work for floors and foundations,
head walls, elevated equipment pads etc.
- Work has started on the two, two acre feet storage
tanks (30% complete).
- Installation of the process equipment (50% complete).
- Installation of site's power requirements (70%
complete).
Work has not yet started on:
1. planting of "tree barrier" adjacent to the Pro-Mark
property
B. Background Regarding Design Changes
At the time of the June 22, 1999, Action Memorandum, it was
determined that as a result of a detailed cost analysis, funds
obligated in the original Action Memorandum of September 30,
1998, were not adequate to proceed very far into the construction
of the plant, much less to complete it or to adequately enter a
"shake-down" period. The June 22, 1999, Action Memorandum
identified two main reasons for the differences in scope and cost
of the removal that supported the consistency exemption and
ceiling increase Action Memorandum. First, during the removal
action design process, U.S. EPA identified areas where technical
issues that were addressed in the original work of the remedial
action contractor needed to be revisited and more thoroughly
addressed than before. Second, during the removal action design
process, new technical issues were identified. These issues were
in areas that had not been previously thought of, but that needed
to be addressed to ensure a protective clean-up and to ensure
that the removal action was conducted in a cost-effective manner
consistent with the remedial action at the Lemon Lane Landfill
site. 2
The differences between the Tetra Tech (Remedial Contractor)
estimate and the Earth Tech (Removal Contractor) costs as
determined after design were explained in the June 22, 1999,
Action Memorandum, and are reiterated in more detail below.
The original rough cost estimate described in the action
memorandum was developed by the Lemon Lane Landfill remedial
contractor in generally analyzing was a broad spectrum of the
various treatment technologies available for the ICS site, and
the various costs of these technologies. This original
assignment was not intended to be used as a design estimate.
Indeed, the time needed to do a design estimate was not given to
the remedial contractor. Rather, the task of developing the
design estimate, along with the design and construction, was
given to the removal contractor.
In considering the differences in both the scope of the project
and the costs between the remedial contractor (Tetra Tech) and
the removal contractor (Earth Tech), it must be noted that the
primary purpose of the remedial contractor (who assisted U.S. EPA
in developing the conceptual outline of this removal action) was
not to provide an engineer's estimate of the cost of the project,
but was simply to compare the cost of the various removal action
options being considered and to assist in identifying a cost
effective alternative. Once the project was assigned to Earth
Tech, the engineering and design was initiated. This work took a
full four months at a cost of $413,000 to produce an engineer's
estimate and, to date, is the only true estimate of the project's
costs. During the course of the design process issues came into
focus that had not been previously considered during the
conceptual phase, but that none-the-less needed to be addressed.
Other issues that were generally considered during the conceptual
phase came into sharp focus requiring, in some instances, a re-
evaluation of (and in some instances changes to) the conceptual
approach.
Thus, at the conceptual stage the following items necessary items
were either not included or not adequately considered:
- No provision for emergency power, critical at "high
flow", if power were to be lost.
- No separation of clean surface runoff from the
contaminated spring water. Maintaining separation of
the clean surface runoff from contaminated spring water
reduces the total amount of water to be treated. The
separation is accomplished through an additional "jack
and bore" of a conduit under the active railroad
tracks. This matter was not considered originally.
- Re-use of the original spring water conduit under the
railroad tracks despite not knowing the structural
integrity of the 24" pipe. The age of the existing
conduit is estimated to be many decades.
- The original 2-acre foot containment was contemplated
to be in the form of a lagoon with a synthetic liner
(as opposed to the storage tanks that have been
designed). The lagoon approach did not take into
account the Karst topography. The lagoon concept also
did not address the removal of accumulated contaminated
sediment, or overflow or by-pass piping.
- No provisions for sanitary sewer, or potable water to
the treatment building.
- Grossly inadequate access road into the site.
- No provisions for concerns of adjacent property owners
i.e. Pro-Mark, with regards to landscaping, sight
barriers, etc.
- No cost provisions for a "shake down" period prior to
the plant being turned over to the State.
The above items, together with the flexibility designed into the
plant (including added electrical capacity, increased pipe
diameters, an additional 2-acre feet of storage, and 40% added
floor space in the treatment building) ensure compatibility with
the final Lemon Lane Landfill remedial action. The above list
includes the predominant reasons for the difference in costs
between the original cost estimate (identified in the Action
Memorandum) and the removal engineer's design estimate.
As explained in the June 22, 1999, Action Memorandum, the
facility currently under construction is not a final remedy.
Rather, it is a "flexible interim remedy" intended to be
consistent with the remedial action at Lemon Lane Landfill.3 The
Plant is designed to make the transition to the future final
remedy as easy as possible and with minimal interruption to the
treatment process. From the larger building to the excess
electrical capacity and piping size, everything is geared toward
not having to add building space or dig up and replace pipelines
or conduits (thereby effectively terminating the plant's
operation) during any final remedy retrofit.4 U. S . EPA
anticipates that the final remedy may call for something
additional, such as pumping capacity or different/extra process
equipment. By scaling the plant today, however, for possible
expansion if necessary, does not result in large short-term
expense (the difference between an 8 inch pipeline and a 10 inch
pipeline, and added electrical capacity is not a substantial
funding increase) and the benefits of scaling the Plant expansion
may result in overall cost savings when compared to failure to
include expandability in the original design and then attempting
a retrofit.5>
Furthermore, the storage tanks are bolted steel tanks that also
can be moved, as can the actual building itself.
C. 25-YEAR STORM EVENT AND FLEXIBLE DESIGN
The flexible design as approved by U.S. EPA has combined the
initial guidelines of 1,000 g.p.m. of water treatment using basic
water treatment technology and a storage of 2 acre feet, with the
addition of more storage capacity. Outside of adding the 2 acre
feet of storage, the U.S. EPA has adhered to the initial
guidelines. U.S. EPA has determined that by designing the ICS
plant to address a 25 year storm event by simply adding 2 acre-
feet of storage capacity and additional assorted pumps and
miscellaneous equipment, is protective of Clear Creek.6 The
1,000 g.p.m. plant, along with ability to send an additional
5,000 g.p.m. to storage (up to 4 acre-feet to be treated off
peak) will be able to remove approximately 70% of the total
sediment of that storm event. Although a 25 year storm event
only holds a 4% chance of occurring at any given time, it comes
down to whether or not such a release is harmful. U.S. EPA has
determined that such an event would be harmful, particularly when
it can be 70% captured with a relatively small additional
financial input.7
U.S. EPA's June 22, 1999, Action Memorandum amended the removal
action to allow for design and construction of a system capable
of addressing storm water flows from a 25-year storm event
(defined as a 3.7" rain in a 6 hour period by the National
Engineering Handbook). This differed from the conceptual
approach of a plant capable of treating contaminated water at a
rate of 1,000 gpm and with the ability to store up to two acre-
feet of water pending treatment.
The amount of PCBs on a mass basis found in the discharged ICS
storm water increases during large storm events. The PCBs are
discharged as part of the suspended solids, or sediment, coming
out of the spring during high-flow events. U.S. EPA's decision
to design the plant to handle the total gallons per minute of a
25-year storm event, together with a removal efficiency of 1
micron of contaminated sediment, was driven, in part, by the fact
that for this relatively small investment of approximately
$350,000 for additional storage capacity, an added degree of
protection for Clear Creek can be achieved and a removal
efficiency of 0.1 to 0.3 ppb (parts per billion)of PCB's, can be
met.
Because of time constraints, driven by a Court Order that
requires the start of the clean-up of the Lemon Lane Superfund
Site (which is hydraulically connected to the spring and the
source of the PCBs emerging from the spring) by the spring of the
year 2000, there was insufficient time to conduct a "particle
size study" before designing and constructing the Plant. Absent
specific the information regarding particle size, there was
insufficient information on which to base a design for a plant
capable of adequately addressing site risks using as a general
design parameter the ability to treat 1,000 g.p.m. of storm water
and capable of 2 acre-feet of storage. Accordingly, U.S. EPA,
based on a consensus of opinions by Earth Tech's design team,
agreed with the recommendation, that it was appropriate to design
the treatment plant to address a 25-year storm event (see
attachment 4). It was understood that the added costs associated
with the addition of an extra two acre-feet of storage, would be
in the range of $350,000 (including adding extra pumps).
To enable the Project to be more cost effective and in lieu of a
particle size study, U.S. EPA also instructed Earth Tech to
design the plant to be capable of removing storm water total
sediment down to a particle size of 1 micron. Below 1 micron,
any suspended sediment is considered colloidal and to remove a
colloid from the spring water would involve flocculation and
coagulation and this technology would be considered "ultra
filtration." It was roughly estimated that to add a flocculation
and coagulation system to the treatment train would add an
additional $1,000,000 to the project costs. Addressing colloids
and the use of ultra-filtration is beyond the scope of this
project, but will be considered in the final remedy selection
process.
U.S. EPA's decision to design the plant to address the risks from
storm water flows during a 25-year storm event (as opposed to the
conceptual 1,000 g.p.m with 2 acre feet of storage approach)
results in the plant's ability to increase its PCB percentage
recovery from an estimated 40% of the PCB mass released during
such an event to 70% of the PCB mass released during a 25-year
storm event. This level of "protectiveness" to Clear Creek was
deemed appropriate and necessary by the U.S. EPA.
U. S. EPA's system has been designed to be protective and will
not permit any water to by-pass the plant for maintenance and/or
equipment breakdowns. In addition, EPA's system will only allow
for by-pass when the total pumping capacity is overwhelmed when
influent volumes exceed 6,000 g.p.m.8 U.S. EPA believes that its
approach is most protective of Clear Creek and is achievable with
the 25 year design.
D. MAJOR DESIGN CHANGES; CONCEPTUAL Us ACTUAL DESIGN
With regards to the storage of storm water pending treatment,
U.S. EPA has determined that the best approach consists of
constructing two above-ground storage tanks, each capable of
storing up to two acre feet of storm water flows from Illinois
Central Spring. This is a shift from the "lagoon" approach
contemplated at the conceptual stage. At the conceptual stage a
lagoon capable of two acre-feet of storage water storage was to
be located in line with the bed of Clear Creek. This "basin"
would be used for both storage of storm water pending treatment,
as well the settling of the suspended solids. During the design
phase of the plant, U.S. EPA determined that the use of a lagoon
in the type situation presented at Illinois Central Spring would
not perform either the storage or the settling features very
well, and that significant risks would be posed if a lagoon were
relied on based on the topography of the area.9
The main reason U.S. EPA abandoned the lagoon concept is the
instability of the Karst topography present throughout boundaries
of the site.l0 Because of the Karst topography, and the various
cracks, vugs and "swallow holes," at the Site, U.S. EPA
determined that significant risks of release of contaminated
materials was presented by reliance on a synthetic liner system
placed on this type of subsurface. Ensuring liner integrity was
determined to be too problematic to warrant proceeding.
Among the other problems identified with the use of a lagoon
system are the following: A limited ability to remove from the
lagoon sediment and foreign material such as leaves, twigs and
other debris without risking the integrity of the liner; extended
periods of time where there lagoon could not be used (unless the
lagoon is compartmentalized) during maintenance work or during
sediment removal, thus placing the stream at risk; concern over
attractive nuisance issues; concern over wildlife exposure to
contaminated sediment accumulated in the lagoon; and, finally,
concern over the ability to detect for rips or tears in the liner
of the lagoon, an item that a double walled bottom of a storage
tank would eliminate.
Abandonment of the lagoon concept (and instead using a storage
tank system) also resolves problems associated with housing,
mounting, and protecting the pumps and assorted electrical
components needed to transport the contaminated water to the
treatment plant. By constructing a spring water receiving sump
and an accompanying small building, this important function now
falls into place.
During design, U.S. EPA also determined that there was a need to
handle sediments collected during the capture and treatment
process. Earth Tech completed a flow diagram showing how the
sediment will be managed by the plant once captured. By use of a
thickener and a filter press, the PCB laden sediment can be
dewatered and shipped off site for disposal. The fact that U.S.
EPA is using a filter press, and providing a means for dealing
with sediments that will result from treatment does not make this
system any less of an interim system. Rather, it recognizes the
potential for large amount of sediment to be released from Lemon
Lane during the Lemon Lane remediation, scheduled to begin in the
spring of 2000, and provides a cost-effective method for
addressing that potential.
The design also provides for an emergency power source to ensure
continued operation in case of a commercial power outage. This
is also needed to ensure that this removal is protective. The
most turbid and contaminated water flow occurs during high flow,
and that high flow probably will happen during a storm event.
Commercial power to the plant is most likely to be interrupted
due to storms. Accordingly, back-up power is appropriate.
U.S. EPA's conceptual approach estimated $24,000 for the access
road and $13,000 for clearing and grubbing of the site. The
actual clearing and grubbing cost for an "8-A" firm was $62,000.
The all weather access road's cost was $71,000. At the
conceptual stage U.S. EPA had erroneously failed to provide power
and utilities, such as natural gas and telephone, and had no
provision for emergency power ($150,000 for a diesel generator).
These expense are for the most part not new, but the were
estimated incorrectly before the design was prepared. In
addition, while these elements are durable, they do not transform
this interim system into a final system. Rather, these are
components that are compatible with both.
Another significant design change involved the manner in which
the contaminated spring water is collected and then transported
to the treatment plant. The conceptual design made no provision
for separating the clean surface runoff from the contaminated
spring water. It also assumed that the decades old conduit under
the adjacent railroad would be adequate to continue to transport
the spring water. It was an easy decision not to treat clean
surface water, which is achieved through construction of an
earthen berm and a separate clean water by-pass. It also
followed logic to construct a new spring water pipe and use the
original pipe as a reserve. Three 2-inch PVC were also run in
the annular space between the casing and the pipe for permanent
electricity, should it be needed at the spring.
One last major design difference was that the conceptual report
included no cost provisions for a "shake down" period before the
treatment plant was turned over to the State. Of course the person who prepared the conceptual report had no way of anticipating that such a agreement would be in place.
IV. EXPECTED CHANGE IN THE SITUATION SHOULD THE ACTION BE
DELAYED OR NOT TAKEN
There most certainly would be an increased risk to public health
and to the environment if the Illinois Central Spring water
treatment plant is delayed or not built. The high levels of PCB
that are currently affecting the Clear Creek ecosystem will
continue to affect the ecosystem and those attempting to use the
resources of the creek downstream.
V. RECOMMENDATION
This memorandum represents a further explanation of the selected
removal action for the Illinois Central Spring Site located in
Bloomington, Indiana, developed in accordance with CERCLA, as
amended, and is not inconsistent with the NCP. This decision is
based upon the Administrative record for the site. Conditions at
the site continue to meet the NCP Section 300.415 (b) (2)
criteria for a removal action and I recommend your approval of
the explanations presented in this document.
APPROVE: Wm. E. Munro
Director, Superfund Division
FOOTNOTES
1 Using the 1996 calendar year, approximately 20% of the
total PCB mass released during the 1996 calendar year is
attributed to non-peak flow discharges and 80% of the total PCB
mass released is during peak or storm flow events. The total
mass of PCBs released during calendar year 1996 is estimated to
be 18.7 kilograms or approximately 41.14 pounds. One pound of
PCBs has the potential to contaminate 454,000 kilograms (or
approximately 998,800 pounds) of stream sediment at a
concentration of greater than 1 ppm PCBs.
2 The plant as designed does not differ conceptually from
the plant as originally conceived in any substantive manner. The
plant, as designed, is capable of treating 1,000 gpm of storm
water flow, as did the conceptual plant. Both plants provided for storm water storage. At the conceptual stage a 2-acre foot lagoon storage system was envisioned. As discussed more fully
later in this memorandum, the lagoon approach was abandoned
during the design process in favor of a 4-acre foot above-ground
storage tank system. The difference in cost between the two
approaches is approximately $350,000.
3 U. S. EPA's system is not a "mobile portable" system that
can be readily moved en masse to a new location. However, all of
the equipment in the process was designed with portability in
mind, as witnessed by the many pipe connections which were
selected for easy disassembly and reassembly if so desired.
Thus, the equipment used in the treatment of storm water (such as
the carbon vessels) can be removed and re-used somewhere else.
4 At the conceptual stage, building costs were estimated at
$45,000. Using a low hypothetical cost of $50 per sq. ft., the
space afforded at the conceptual stage would be in a 30' x 30'
building. This size building would be far too small even for the
treatment process that was being considered at the conceptual
stage, and did not include costs for things like foundation
costs, wiring, piping, etc. U.S. EPA's building, as designed
will be able to house the added thickener and filter press along
with space to house on office, and a small laboratory with
lavatory.
The building also contains 40% added space above and beyond what
will be used by the Earth Tech process. This added floor space
is projected to be used in the "final remedy" phase perhaps
to house the "ultra filtration" equipment and is part of the
"flexible remedy" that U.S. EPA has designed for in its project.
The cost of the building "as built," including costs for
foundation, piping, wiring, etc., is approximately $2,048,500.
The cost of the additional 40% space is approximately $281,700,
or approximately 14% incremental additional cost.
5 A final design will be approved as part of the final
treatment system. That design may include various water
treatment technologies that can be best described as "ultra
filtration". This technology, will involve either (or both)
reverse osmosis or flocculation/coagulation, in addition to the
processes that will be in place. For any new technology to be implemented, certain piping, power, and building requirements will have to be met. It makes sense to design and build to those
requirements now where significant costs savings will be realized
and the cost of retro-fit avoided. The capital cost of a 10"
pipeline does not differ significantly from that of a 12"
pipeline. This also holds true for added electrical capacity and
additional square feet of building space. These three items
demonstrate that the Illinois Central Spring water treatment
plant will be able to transition from a "flexible to a final"
plant with little or no impact on its operation and with little
additional costs, other than potential additional treatment
equipment costs.
6 In the 1998 action memorandum, U.S. EPA determined that a
two-acre feet storage system would be sufficient for storm water
flows. U.S. EPA in part founded its decision in this regard
based on data regarding one isolated year of storm data. Earth
Tech reviewed charts and data from CBS and determined that it is
more appropriate to design a system capable of addressing storm
water flows during a 25-year storm event. A 25 year storm event
is a common event to design to and has been used by other
government agencies.
7 More than only low flows need to be addressed to protect
Clear Creek, and a portable system simply would not be able to
handle high flows. A portable plant of the kind CBS suggested in
its June 1, 1999, proposal, cannot adequately protect Clear Creek.) A portable system might remove PCB's coming from the
spring during low flow, but low flow is not the concern. The
turbidity of the spring water increases as the severity of storm
events increase, thus increasing PCB concentrations during high
flow. This is the period where the operation of the plant is
most critical from the standpoint of protecting Clear Creek.
U.S. EPA's "flexible design" plant will handle high flow where a
portable plant cannot.
U.S. EPA's flexible interim design plant has a 1000 g.p.m.
treatment capacity. However, U.S. EPA's plant also will be able
to concurrently send an additional 5,000 g.p.m. to storage (up to
four acre feet) for treatment after the storm surge diminishes
(25-year storm event). A portable plant would have to allow
untreated storm water flow by-passes to Clear Creek and, thus,
all of the PCBs contained in the suspended sediment that is known
to emanate from the spring during a storm, would go untreated
directly to Clear Creek. To stop the treatment process at 1,000
g.p.m. without a storage and settlement train in the treatment
process will allow more PCB sediment to enter Clear Creek during
one storm event than a low flow portable plant could capture in
many months of operation at low flow.
8 The main purpose for the plant is to capture the maximum
amount of PCB sediment released during a storm event or high
flow, as the amount of suspended solids released during low flow
is minor when compared to a high flow situation. To maximize the
amount of PCB sediment laden water that can be treated during a
storm event, U.S. EPA decided to partition off the surface
runoff from the spring runoff at the site of the spring
emergence. Because the spring is located in a valley, this can
be simply done by constructing a storm water separation wall
which will greatly reduce the amount of clean surface runoff that
otherwise would be mixing with the contaminated runoff during a
storm event. The clean surface water will be routed untreated to
the Clear Creek at a location down stream from the plant, via a
24" bypass, while the water containing the PCB sediment will
proceed to the plant via its own 24" pipeline. Accordingly, U.S.
EPA has considered the matter of capacity and has taken those
steps that are cost effective to reduce the total volume of water
that needs to be treated. U.S. EPA decided not to trust the
integrity of the decades old conduit under the railroad tracks of
the Indiana Central Railroad and, therefore, constructed two
"jack and bores", one the 24" clean water by-pass and the other
the 24" contaminated spring water pipeline, at a cost of
$150,000.
9 The location of the Illinois Central Spring plant is not
at the location of Illinois Central Spring itself. Rather, the
water is being pumped from the Illinois Central Spring to the
location of the plant. The same scenario can be applied to any
water that might emerge at Quarry Spring or even at the site of
Lemon Lane Landfill - it can be conveyed to the treatment plant
and treated there. A simple receiving sump or receiving sumps,just like the one to be constructed at Illinois Central Spring
can address this issue.
Further, the plant had to be located somewhere. The fact that
the City of Bloomington owned a piece of property that it was
willing to make available without cost to U.S. EPA, that was
isolated, the right size, and that was easily accessible for
construction, are among the reasons the plant was located where
it is.
The Quarry Spring location advocated by CBS property is private
property. Thus, long acquisition negotiations and/or
condemnation proceedings could be anticipated. Further, given
the area and nature of the Quarry Spring location it is likely
that the City and/or the residents might not want either the
plant or the construction traffic there.
10 U.S. EPA has not been presented with any geophysical
work that contradicts U.S. EPA's work and its conclusion that it
is unsound to rely on a lagoon built on karst for storm water
storage.