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RK'S OFFICE
1401 2 1 2007
BEFORE THE ILLINOIS POLLUTION CONTROL BOARD
?
STATE
OF
ILLINOIS
Pollution Control
Board
ORIGINAL
AS
ye-
.„0(1/

(Adjusted Standard –Land)
(Waste Delisting)
IN THE MATTER OF:
PETITION OF BFI WASTE SYSTEMS
OF NORTH AMERICA, INC. FOR AN
ADJUSTED STANDARD WASTE
DELISTING
NOTICE OF FILING
To:
?
Robert A. Messina, Chief Legal Counsel
Division of Legal Counsel
Illinois Environmental Protection Agency
1021 North Grand Avenue East
Post Office Box 19276
Springfield, IL 62794-9276
Mary A. Gade, Regional Administrator
U.S. Environmental Protection Agency
Region 5
77 West Jackson Boulevard
Chicago, IL 60604
Mr. Douglas Scott, Director
Illinois Environmental Protection Agency
1021 North Grand Avenue East
Post Office Box 19276
Springfield, IL 62794-9276
(Without Attachment A)
Mr. Bill Child, Bureau Chief
Bureau of Land
Illinois Environmental Protection Agency
1021 North Grand Avenue East
Post Office Box 19276
Springfield, IL 62794-9276
(Without Attachment A)
Please take notice that on November 21, 2007, the undersigned caused to be filed with the Clerk
of the Illinois Pollution Control Board the attached BFI Waste Systems of North America, Inc. Petition
for Adjusted Standard Waste Delisting and Motion to File Reduced Number of Copies, copies of which
are herewith served upon you.
By:?
atricia F. Sharkey
Patricia F. Sharkey
McGuireWoods LLP
77 West Wacker Drive, Suite 4100
Chicago, Illinois 60601
Telephone: 312/849-8100
Attorney Reg.: 6181113

 
Patrici. F. hark
y
CERTIFICATE OF SERVICE
RECEIVED
CLERK'S OFFICE
NOV 2 1 2007
STATE OF ILLINOIS
Pollution
Control Board
I, Patricia F. Sharkey, one of the attorneys for BFI Waste Systems of North America, Inc., hereby
certify that I served a copy of the Petition for Adjusted Standard Waste Delisting and Motion to File
Reduced Number of Copies upon those listed on the attached Notice of Filing on November 21, 2007 by
depositing the same in the U.S. Mail, with First Class prepaid postage, at 77 West Wacker Drive,
Chicago, Illinois 60601.
McGuireWoods LLP
77 West Wacker Drive, Suite 4100
Chicago, Illinois 60601
Telephone: 312/849-8100
ORIGINAL
\4883063.1

 
RECEIVED
CLERK'S
OFFICE
BEFORE THE ILLINIOS POLLUTION CONTROL BOARD
Plc,'
2
1 2007
STATE
-
OF
Control
ILLINOISBoard
IN THE MATTER OF:
(2(‘'
1
AS Olt
(Adjusted Standard -Land)
(Waste Delisting)
PETITION OF BFI WASTE SYSTEMS
Ci R
?
C
I
OF NORTH AMERICA, INC. FOR AN
ADJUSTED STANDARD WASTE
DELISTING
Motion to File Reduce Number of Copies
NOW COMES BFI Waste Systems of North America, Inc. ("BFI"), by its
attorneys McGuireWoods LLP, and moves the Illinois Pollution Control Board ("Board")
to allow the filing of a reduced number of copies (four plus an original) of the Weaver
Boos Technical Support Document, Attachment 1 to the BFI Waste Systems of North
America, Inc. Petition for Adjusted Standard Waste Delisting.
In support thereof, BFI states:
1.
Board regulations require that for any document filed with the Board, the
filing party must file nine copies plus an original. 35 Ill. Adm. Code 101.302(h).
2.
BFI is today filing nine copies and an original of its Petition for Adjusted
Standard Waste Delisting and all attachments with the exception of Attachment 1, the
Weaver Boos Technical Support Document.
3.
Because each copy of the Technical Support Document includes
approximately six inches of materials, contained in two separate three-ring binders, BFI
is requesting that the Board allow it to file four copies plus an original of the Weaver
Boos Technical Support Document.

 
WHEREFORE, BFI requests that the Board grant this motion to allow the filing
of a reduced number of copies of the Weaver Boos Technical Support Document,
Attachment I to the Petition for Adjusted Standard.
Respectfully submitted,
BFI Waste Systems of North America, Inc.
By One of Its Attorneys
Patricia F. Sharkey
McGuireWoods LLP
77 West Wacker Drive, Suite 4100
Chicago, Illinois 60601
312/ 849-8100
Attorney Reg: 6181113

 
CR I
G
I \
NOV 21 2007
STATE OF ILLINOIS
Pollution Control
Board
(Adjusted Standard —Land)
(Waste Delisting)
ED
BEFORE THE ILLINOIS POLLUTION CONTROL BOARD
?
ICE
IN THE MATTER OF:
PETITION OF BFI WASTE SYSTEMS
OF NORTH AMERICA, INC. FOR AN
ADJUSTED STANDARD WASTE
DELISTING
PETITION FOR ADJUSTED STANDARD
WASTE DELISTING
NOW COMES BFI Waste Systems of North America, Inc. ("BFI"), by its
attorneys McGuireWoods LLP, pursuant to Section 28.1 of the Illinois Environmental
Protection Act ("Act"), 415 ILCS 5/28.1, 35 Ill. Adm. Code Part 104, and 35 Ill. Adm.
Code 720.122 (40 CFR 260.22), and petitions the Illinois Pollution Control Board
("Board") to grant an adjusted standard delisting landfill leachate generated at the closed
Phase I Unit at BFI's Davis Junction Landfill.
INTRODUCTION
BFI is petitioning to delist leachate generated at the long-closed Phase I Unit at its
Davis Junction Landfill in Davis Junction, Ogle County, Illinois.' Under the proposed
Adjusted Standard, the management of the leachate at the Davis Junction Landfill will
continue to be governed by the Illinois RCRA Post-Closure Permit, however, BFI will be
allowed to transport and dispose of the leachate as a non-hazardous Illinois special waste.
The delisting will apply to leachate collected at the Phase I Landfill Unit ("Phase I Unit")
over the remaining RCRA Post-Closure Period which is anticipated to be seven years,
The Davis Junction Landfill also includes two other closed landfill units ( Phase II and III) that accepted
solely municipal solid waste ("MSW"). The Phase I Unit is separated from the two closed MSW units
(Phases II and III) by a clay berm and has completely separate leachate collection and storage systems. This
petition pertains solely to the leachate generated in the Phase I Unit.
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1

 
although this could be extended by the Illinois Environmental Protection Agency
("IEPA"). The maximum volume of leachate that is anticipated to be generated is less
than 500,000 gallons per year.
The Phase I Unit leachate is currently classified as F039, a listed hazardous waste
from non-specific sources under 35 IAC 721.131 (40 CFR 261.31(a)). F039 listed
hazardous waste is defined as "leachate (liquids which have percolated through land
disposed wastes) resulting from the disposal of more than one restricted waste classified
as hazardous under Subpart D." In this case, the Phase I Unit leachate is considered a
hazardous waste due to the historic disposal of minor volumes of hazardous wastes (2%)
within the Phase I Unit.
The leachate collected at the Phase I Unit is pumped via hard-pipe to a temporary
holding tank with secondary containment and then hauled off-site for disposal. The
leachate is not treated before disposal. It also is not stored in on-site impoundments or
conveyed via on-site ditches.
Because there is no domestic sewage sewer system connecting the Davis Junction
Landfill to a local waste water treatment facility ("WWTF"), this leachate cannot be
disposed of pursuant to the RCRA domestic sewage exemption in 35 Ill. Adm. Code
721.104(a)(1) (corresponding to 40 CFR 261.4(a)(1)). (See U.S. EPA's "Little Known
But Allowable Ways to Deal with Hazardous Waste," EPA 233-B-00-002, May 2000.)
As a result of its classification as F039 and the absence of a local sewer system,
the leachate collected at the Phase I Unit must be disposed of at a hazardous waste
disposal facility authorized to accept hazardous liquids. The closest facility authorized to
accept liquid hazardous waste is the CID Recycle and Disposal ("CID") facility in
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2

 
Calumet City, Illinois, over 100 miles from the Davis Junction Landfill. Should that
facility become unavailable, the next closest liquid hazardous waste disposal facility is
located in Ohio, 365 miles from the Davis Junction Landfill.
Hauling the Phase I Unit leachate this great distance is expensive. It also wastes
energy, pollutes the air with diesel emissions, and increases the risk of highway accidents
that could result in a release to the environment. In contrast, the leachate generated at the
other two closed non-hazardous landfill units at the Davis Junction Landfill ( Phase II and
III) is hauled to the Interstate Pollution Control, Inc. ("IPC"), a centralized waste water
treatment plant that chemically treats the leachate prior to discharge to a publicly owned
waste water treatment facility ("POTW"). IPC is located on the outskirts of Rockford,
only seven miles from the Davis Junction Landfill. This delisting would allow BFI to
haul the Phase I Unit leachate to the IPC facility or another similarly equipped and more
local facility. It would be hauled in the same manner as BFI currently hauls the Phase II
and III Unit leachate, pursuant to an Illinois Special Waste manifest.
The constituents in the leachate are well known. BFI has monitored the leachate
itself, as well as groundwater beneath the landfill, as required by the Illinois RCRA
landfill program for over twenty-five years. The leachate data for the last nine years is
included in
Appendix
C
of the Technical Support Document (Attachment 1 hereto)
("Technical Support Document").
A summary of that data is shown in the
Comprehensive Constituent List in
Appendix D.
A summary of the Davis Junction
Landfill groundwater monitoring results is included in
Appendix J.
For purposes of this delisting, BFI has evaluated the leachate data collected over
the last nine years. This time period was selected because a new cap was installed in 1998
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3

 
and thus the post-1998 data is most reflective of current conditions and most indicative of
future leachate quality and quantity. This evaluation includes several thousand individual
data points. See
Appendix D, Technical Support Document.
At Illinois EPA's suggestion, BFI compared this data to the monitoring data for
the leachate generated by its non-hazardous Phase II and III landfill units. The fact that
the constituents in the Phase I, II and III units are generally consistent in both nature and
concentration, with the exception of a few constituents, supports the conclusion that this
delisting is appropriate. (See side-by-side comparison in
Appendix D of the Technical
Support Document).
Those constituents that differ and whether they warrant retaining
this leachate as a hazardous waste are discussed in greater detail below in
Section 9 of
the Technical Support Document.
The length of time over which this leachate has already been monitored provides
assurance that the quality of the leachate has stabilized. The type of hazardous
constituents in the leachate has not significantly changed over nine years. To the extent
there is variability in the concentrations of constituents, that variability is not statistically
significant. See
Appendix D of the Technical Support Document.
In recent years, the volume of leachate generated at the Phase I Unit has declined
substantially from 468,300 gallons in 2002, to an annual average of 285,000 gallons for
the four years of 2003 through 2006. The volume projected for 2007 is approximately
250,000 gallons. See
"Table 1 – Annual Hauling Date," Technical Support
Document.
Declining volumes are expected because the landfill has been closed and
capped for over twenty-four years. No new hazardous wastes have been introduced since
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4

 
1983. Furthermore, no new hazardous wastes will be introduced in the future and the
approved RCRA cap and liner assure that no outside contaminants enter the landfill.
Notwithstanding the fact that leachate production will naturally decline
throughout the post-closure period, BFI endeavors to maximize leachate extraction in
order to expedite final closure of the Phase I Unit. Increased leachate extraction can be
achieved through active maintenance of the wells and pumps. For example, the volume
of leachate generated in 2006 increased as a result of well replacement and installation of
a new force main. Even maximizing leachate extraction, leachate volumes from the Phase
I Unit are not expected to exceed 500,000 gallons per year in the future.
The duration of the proposed delisting will coincide with the duration of leachate
collection regulatorily required by the RCRA Post-Closure Permit. Under that permit, the
groundwater and leachate are already subject to annual monitoring. The proposed
Adjusted Standard will increase monitoring of the leachate for the identified constituents
of concern from annual monitoring to quarterly monitoring in the first year and semi-
annual monitoring thereafter. This monitoring will provide both initial and on-going
assurance that the qualitative nature of the leachate does not exceed the proposed
delisting levels.
A.?
Standard of General Applicability from Which Adjusted Standard is
Sought (35 III. Adm. Code 104.406(a))
The standard of general applicability from which this Adjusted Standard is sought
is the Illinois regulation classifying the Phase I Unit leachate as a hazardous waste.
Because the Phase I Unit accepted a small amount of one or more hazardous wastes
during its operating life, the leachate generated at the Phase I Unit is currently classified
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5

 
as a listed hazardous waste from non-specific sources pursuant to 35 III. Adm. Code
721.31(a) . Specifically, this leachate is classified as "F039 – Leachate (liquids that have
percolated through land disposed wastes) resulting from the disposal of more than one
restricted waste classified as hazardous under Subpart D of this Part.)" As a result of this
classification, this leachate must be handled and disposed under the requirements of 35
Ill. Adm. Code Parts 720 – 728.
B.
Statutory Basis of Regulation of General Applicability (35
Ill.
Adm. Code
104.406.(b))
The Illinois hazardous waste regulations, including 35 Ill. Adm. Code Parts 720 -
728, were promulgated to implement the requirements of the federal Resource
Conservation and Recovery Act of 1976 and the federal regulations at 40 CFR Parts 260-
268. Specifically, the F039 hazardous waste classification 35 Ill. Adm. Code 721.31(a) is
identical in substance to the federal F039 classification in 40 CFR 261.31(a).
C.
Level of Justification Specified by Regulation of General Applicability
( 35
Ill.
Adm. Code 104.406(c))
Section 720.122 of the Illinois regulations, 35 Ill. Adm. Code 720.122, reflects the
requirements for delisting of a hazardous waste established in the federal RCRA
regulations at 40 CFR 260.22. A person seeking to exclude a waste from a particular
generating facility from the lists of listed hazardous waste contained in Subpart D of 35
Ill. Adm. Code 721 must file a petition meeting the requirements specified in 720.122(n)
and such petition must be found by the Board to demonstrate the following:
1. That
the waste produced by the particular generating facility does
not meet any of the criteria under which the waste was listed as a
hazardous or acute hazardous waste. (35 Ill. Adm. Code 720.122(a)(1));
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6

 
2.
That there is a reasonable basis to believe that factors (including
additional constituents) other than those for which the waste was listed
could cause the waste to be a hazardous waste, that such factors do not
warrant retaining the waste as a hazardous waste. A Board determination
under the preceding sentence must be made by reliance on, and in a
manner consistent with, "EPA RCRA Delisting Program--Guidance
Manual for the Petitioner," incorporated by reference in Section
720.111(a). (35 In Adm. Code 720.122(a)(2)); and
3.
That a waste so excluded is not hazardous waste by operation of
Subpart C of 35 Ill. Adm. Code 721, i.e. is not a hazardous waste by virtue
of exhibiting one of the hazardous characteristics specified in Subpart C.
(35 Ill. Adm. Code 720.122(a)(2))
D. Nature of Petitioner's Activity ( 35
Ill.
Adm. Code 104.406(d))
1. Nature of Activity
As discussed in the introduction above and in greater detail in the
Technical
Support Document,
BFI collects leachate generated pursuant to the closure requirements
of an Illinois RCRA Post-Closure Permit (No. B-142-M-10 and M-11) at the closed
Phase I Unit which accepted minor amounts of hazardous waste during its seven year
operating life, i.e. from December 1976 through January 1983. The Phase I Unit was
certified closed on December 5, 1984.
Detailed records of the nature and volume of hazardous wastes disposed of in the
Phase I Unit have been kept. Those records demonstrate that 87% of the waste received
was general municipal refuse, 11% was special waste, and the remaining 2% was
considered hazardous waste. The total volume of waste placed in the Phase I Unit was
approximately 1,900,000 cubic yards. Approximately 26,000 cubic yards (less than 2
percent) of that waste was defined as hazardous under RCRA and state law.
Of the 2% hazardous waste disposed of in the Phase I Unit, approximately 96%
consisted of heavy metal sludges and the remaining 4% consisted primarily of spent
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7

 
solvent still bottoms, spent solvent sludges, petroleum refining residues, rodenticides,
glycol, polystyrene, and pthalic anhydride. Specific information regarding the generator
and quantities of each listed waste is included in
Appendix
A of the
Technical Support
Document.
Notably, the constituents in the Phase I Unit leachate closely resemble the
constituents in the leachate generated at the Phase II and III Units, which BFI has also
monitored for many years and which is not classified as a hazardous waste. See
Appendix D
of the
Technical Support Document.
The fact that the Phase I Unit
leachate is not qualitatively different from the Phase II and II Units' leachate, supports
the conclusion that the costs associated with handling this leachate as a hazardous waste
are unwarranted.
Currently, the Phase I Unit leachate is transported for disposal by tanker truck to a
permitted RCRA liquid hazardous waste treatment facility, the CID Facility at 138
th and
Bishop Ford Expressway in Calumet City, over 100 miles away. This delisting would
allow the transportation and disposal of this leachate as an Illinois Special Waste at a
closer waste water treatment facility, such as the "IPC" facility, which is located just
seven miles from the landfill. BFI hauls the leachate from its non-hazardous Phase II and
III Units to IPC. This Adjusted Standard will not only reduce costs, but will also reduce
the use of diesel fuel, reduce the emissions generated by the over 200 mile roundtrip
required to haul this waste to CID, and reduce the risk of a highway accident resulting in
a release of the leachate directly to the environment.
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8

 
2.?
Location of and Area Affected by Petitioner's Activity
Location:
Davis Junction Landfill — Phase I Unit
8902 N. Route 251
Davis Junction, Ogle County, Illinois 61020
RCRA ID Number: ILD980700751
Affected Area:
The Phase I Unit occupies approximately 29.5 acres which was operated as a
combined municipal solid waste (MSW) and RCRA Subpart C waste disposal facility.
The Davis Junction Landfill as a whole occupies approximately 160 acres. See
Figure 1
in the Technical Support Document.
The area immediately surrounding the Phase I
Unit and the Davis Junction Landfill is predominantly farmland dotted with farm
buildings. The landfill is located in Ogle County approximately one mile south of the
Winnebago County line. The closest town is Davis Junction located approximately two
miles to the south. Illinois Highway 20 and the outskirts of the City of Rockford are
approximately four miles to the north. Interstate 39 is located approximately two miles
east of the landfill.
The landfill adjoins Illinois Route 251 and the landfill truck entrance is located on
Scott Road, just west of Route 251. (See the
Technical Support Document), Figure 1
(Topographic Map showing facility location) and
Figure
2
(Site Layout — including
location of Phase I Unit). The over 100 mile route over which the Phase I Unit leachate
currently must be transported is shown in the attached MapQuest route map.
Attachment
2
hereto.
For comparison, the seven mile route over which the delisted
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9

 
leachate could be transported to Interstate Pollution Control (IPC) on the outskirts of
Rockford is shown in the attached MapQuest route map.
Attachment
3
hereto.
3.
Age of the Facility and Number of Employees
The Phase I Unit began operation in 1976 and thus is 31 years old this year. Two
BFI employees oversee Post-Closure activities at the closed Davis Junction landfill site.
In addition, the BFI hydrogeology, engineering and finance groups located at other BFI
facilities have responsibilities pertaining to the Davis Junction Landfill site. BFI also has
a number of consultants and contractors, including the landfill gas contractor, who
perform monitoring and maintenance activities at the closed landfill site.
4.
Pollution Control Equipment Already in Place
As is discussed in greater detail in the attached
Technical Support Document,
the closed Phase I Unit is capped and lined. The original leachate collection system began
operation in 1982. An upgraded leachate collection and extraction system was completed
in 1998 -1999. The leachate is not treated on-site nor is it stored in on-site
impoundments, conveyed via on-site ditches or otherwise placed on the ground. Rather,
the Phase I Unit leachate collection system conveys the leachate via hard-pipe to a RCRA
permitted storage tank with secondary containment. Under this delisting, the on-site
handling and storage of the Phase I Unit leachate would remain subject to RCRA
hazardous waste requirements and pollution control equipment.
Pursuant to the conditions in the proposed Adjusted Standard, the Phase I Unit
leachate would be transported and disposed of as a non-hazardous Illinois Special Waste,
as defined in 35 111. Adm. Code Part 808, as is the similar leachate generated at the Davis
Junction Phase II and III Units. As an Illinois Special Waste, off-site transportation of the
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10

 
leachate would be subject to Illinois Special Waste hauler permitting and manifesting
safeguards in 35 Ill. Adm. Code Part 809.
The proposed Adjusted Standard also requires that the delisted leachate be
disposed of at a permitted waste water treatment facility. At an industrial waste water
treatment plant, such as the IPC facility in Rockford, the leachate would be subject to a
chemical treatment process prior to discharge to a POTW. IPC's discharge must meet the
requirements for a significant user waste water discharge authorization prior to being
discharged to the POTW. At the POTW, the treatment technologies and pollution
controls required for the POTW to achieve its Clean Water Act NPDES discharge limits
must be in place.
5. Qualitative and Q uantitative Description of the Emissions, Discharges or
Releases Currently Generated by Petitioner's Activity
The activity of hauling and disposing of the Phase I Unit leachate at a waste water
treatment plant, such as either the CID facility or a more local treatment facility, is an
environmentally sound approach to leachate disposal. Both of these options provide for
more pre-treatment of the leachate than is applied to leachate which is generated at
landfills that discharge directly to a sewer system pursuant to the RCRA domestic sewage
exemption in 721.104 (40 CFR 261.4(a)). It also is a more environmentally protective
approach to disposal than the use of an on-site impoundment.
Although the current leachate disposal at CID does not adversely impact
groundwater because the ultimate discharge to the environment is treated to NPDES
discharge requirements, the long distance hauling of the leachate does result in emissions
to the environment, including carbon dioxide, nitrogen oxide, volatile organics,
particulate, Hazardous Air Pollutants, and carbon black (known as "soot"). Those
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11

 
emissions can be quantified on a per mile basis using standard emission estimates for
mobile source diesel fuel combustion. While the amount of emissions will vary with the
efficiency of the vehicle's engine and pollution control equipment, it is obvious that the
longer the hauling distance is, the greater the volume of emissions will be.
E. Efforts Necessary to Comply with Regulation of General Applicability
(35
Ill.
Adm. Code 104.406(e))
As discussed above, the Phase I Unit leachate, as a F039 hazardous waste, is
currently required to be transported for disposal to a permitted RCRA liquid hazardous
waste treatment facility. The closest such facility is the CID Recycle & Disposal Facility
("CID") at 138 th and Bishop Ford Expressway in Calumet City, over 100 miles away.
This delisting would allow the disposal of this leachate at a closer NPDES permitted
waste water treatment facility, such as the Interstate Pollution Control, Inc. ("IPC")
facility, which is located less than 10 miles from the landfill.
As stated in the 2006 Revised Post-Closure Care Estimates for the Phase I Unit,
the cost of leachate transportation and disposal is approximately $0.338 per gallon of
leachate disposed, while the cost of disposal for leachate designated as non-hazardous
special waste is $0.045 per gallon (based upon the 2006 post-closure financial assurance
estimate for disposal of the non-hazardous waste leachate generated at the Phase I and II
Units). That would mean an annual cost savings of approximately $29,300 for every
100,000 gallons of waste water generated (RCRA Permit No. B-142). At the estimated
maximum annual leachate extraction of 500,000 gallons, this would be an annual savings
of $146,500.
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12

 
Other theoretically available alternatives for the disposal of the Phase I Unit
leachate include: 1) disposal at another hazardous waste disposal facility; 2) construction,
operation and permitting of an on-site treatment facility or underground injection well; or
3) construction of a sewer system to convey the leachate to a waste water treatment
facility. Regarding the first alternative, BFI has been unable to identify a permitted
hazardous liquids disposal site that is closer than the CID facility in Calumet City. The
next closest permitted liquid hazardous waste disposal facility is located in Ohio, 365
miles from the Davis Junction Landfill. Both the second and third alternatives, while
theoretically feasible, would involve substantial capital and operating expenditures to
permit, build and run entirely new on-site treatment and/or disposal facilities.
While liquid hazardous waste can be disposed of below the lowest drinking water
aquifer via a properly permitted Class I underground injection well, such wells have the
potential to adversely impact drinking water resources and require the presence of
suitable geologic formations. All Class I hazardous waste injection wells disposing of a
RCRA land-banned hazardous waste must either complement the well permit with a
rigorous technical demonstration referred to as a "No-Migration Demonstration" or treat
the waste to approved safe levels before disposal. Notably, Illinois has only four such
wells in the entire state.
See Illinois EPA Underground Injection Control Program Web
Page.
Construction of on-site liquid hazardous waste treatment units would require that
BFI duplicate the treatment technologies of a waste water treatment facility like IPC for a
relatively small volume of waste water. Given the fact that the IPC facility is located just
seven miles from the Davis Junction Landfill, the construction, permitting and operation
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13

 
of a separate waste water treatment facility to perform the same function would be a
waste of resources.
The use of these costly and potentially risky alternatives is particularly
unwarranted at a closed landfill with a limited remaining post-closure period. It is also
unwarranted in light of the fact that the Phase I Unit leachate is very similar to the Phase
II and III leachate which is classified
as
non-hazardous and which can be disposed of at a
nearby NPDES permitted waste water treatment facility without pre-treatment or other
capital expenditures.
F.?
Proposed Adjusted Standard (35 III. Adm. Code 104.406(f))
1.?
Proposed Language
BFI proposes that the Board adopt an Adjusted Standard based on the following
conditions or such other conditions as the Board deems appropriate to achieve the relief
sought under this petition:
"Leachate generated at the closed Phase I Unit at the BFI Waste Systems of North
America, Inc. Davis Junction Landfill in Davis Junction, Ogle County, Illinois
shall not be deemed a hazardous waste pursuant to 35 Ill. Adm. Code 721 under
the following circumstances:
a)
The Phase I Unit is subject to an Illinois Environmental Protection Agency
RCRA Post —Closure Permit which prohibits the disposal of any new solid or
liquid waste in the Phase I Unit, requires maintenance of the landfill cap and liner,
and requires operation of a leachate collection system;
b)
The leachate is be hard-piped directly from the landfill to an on-site
storage tank which is regulated under the RCRA Post-Closure Permit and is not
stored or managed in a surface impoundment, conveyed by ditches or otherwise
managed prior to transportation for off-site disposal;
c)
The leachate does not exhibit any characteristic of hazardous waste as
defined in 35 Ill. Adm. Code 721.121, 721.122, 721123 and 721.124 and shall not
exceed the delisting level concentrations in Table A below;
Printed On Recycled Paper
14

 
d)
Within the first 12 months following the effective date of this delisting,
BFI performs quarterly testing of a representative sample of the leachate for the
constituents listed in Table A (below) and hazardous characteristics as defined in
35 Ill. Adm. Code 721.121, 721.122, 721123 and 721.124. If none of the delisting
levels in Table A are confirmed to be exceeded, such testing shall continue on a
semi-annual basis thereafter. If an initial sample concentration is observed above
the delisting level, then a verification sample will be collected within 7 days and
reanalyzed for the constituent(s) exhibiting a concentration greater than the
delisting level. A confirmed exceedance of the delisting level will be deemed
present if both the original and verification sample exhibit concentrations above
the delisting level;
e)
If concentrations of the constituents listed in Table A (below) are
confirmed to exceed the delisting levels using the verification procedures
described above in item (d) or if the leachate is confirmed to exhibit a hazardous
characteristic, the leachate shall not be disposed of except as a hazardous waste
until such time as it is demonstrated by the testing procedures below to meet the
criteria of this Adjusted Standard. Prior to re-initiating management and disposal
pursuant to this Adjusted Standard, BFI must perform additional testing, including
a minimum of four representative samples taken over not less than a 14 day
period, each of which confirms concentrations of F039 hazardous constituents
below the delisting levels and the absence of any hazardous characteristic;
g)
The leachate is transported in compliance with the requirements applicable
to an Illinois Special Waste (35 III. Adm. Code Part 809) to a permitted waste
water treatment facility located in Illinois and subject to the requirements of either
Section 307(b) or Section 402 of the federal Clean Water Act prior to discharge;
h)
At least 60 days prior to transporting the first load of delisted leachate,
BFI shall provide a one-time written notification to the Illinois Environmental
Protection Agency stating that it is commencing transportation of delisted
leachate pursuant to this delisting and the name of the waste water treatment
facility to which the leachate will be transported. If BFI changes disposal
facilities, it shall provide to Illinois Environmental Protection Agency a one-time
written notification of such change; and
i)
BFI shall not transport the leachate delisted pursuant to this Adjusted
Standard outside of the State of Illinois.
Table A
Arsenic
0.525
Barium
151
Benzene
0.153
Cadmium
0.409
Carbon Disulfide
118
Chromium
1,040
Printed On Recycled Paper
15

 
Dichloropropene, cis-1, 3-
1,000,000
Cobalt
118
Copper
24,700
Diethyl phthalate
1,270
Endrin
32,700
Ethylbenzene
57.2
lsobutyl alcohol
299
Lead
204
Mercury
0.22
Methanol
499
Methyl ethyl ketone
599
Methylene chloride
0.198
Methyl isobutyl ketone
79.8
Naphthalene
6.51
Nickel
76.8
Cresol, p-
5.37
Phenol
645
Styrene
6.2
Tetrachloroethylene
0.174
Tin
1180
Toluene
40.2
Trichloroethy lene
0.164
Vanadium
57.1
Vinyl chloride
0.2
Xylenes (total)
886
Zinc
760
Dichloroethane, 1-1-
99.8
Dichloroethane, 1,2-
0.0354
Dioxane, 1,4-
100
Trichlorophenoxypripionic acid, 2,4, 5- (Silvex)
1.43
Dichlorophenoxyacetic acid, 2,4- (2,4-D)
1.86
Dimethylphenol, 2,4-
27.6
Acetone
99.8
2.
?
Narrative Discussion of Proposed Adjusted Standard Language
The proposed Adjusted Standard addresses only leachate generated at the Phase I
Unit of the Davis Junction landfill. The scope of the Adjusted Standard is also limited to
leachate generated while the Phase I Unit is subject to a RCRA Post-Closure Permit. This
limitation provides assurance that the quality of the leachate, which has already been
demonstrated to be stable, will not vary because the RCRA Post-Closure Permit prohibits
the disposal of any new waste, requires the maintenance of the existing landfill cap and
liner, and also requires the operation of a leachate collection system. The Adjusted
Printed On Recycled Paper?
16

 
Standard also provides assurance that the Phase
I
Unit leachate will continue to be
managed on-site at the Davis Junction Landfill by way of a RCRA permitted leachate
collection system and a RCRA permitted storage tank ( Tank #1). The Adjusted Standard
will not allow the leachate to be managed in a land impoundment, ditch or by any other
means which could result in contamination of the leachate and/or a release of the leachate
directly to the environment.
The proposed Adjusted Standard is limited in duration to the time during which a
RCRA Post-Closure Permit requires operation of a leachate collection system. This is
anticipated to be approximately seven years; however, BFI
requests that no absolute time
limit be established in the Adjusted Standard because Illinois EPA may require that the
leachate collection system continue to operate for a longer period of time than BFI
currently anticipates.
The proposed Adjusted Standard requires that a representative sample of the
leachate be tested quarterly for the first year and semi- annually thereafter for a list of
hazardous constituents which are listed in Table A. This testing regimen is consistent
with, and in fact more stringent than, the initial quarterly and subsequent annual testing
that U.S.EPA has required in similar delistings.
See Shell Oil Company - Deer Park,
Texas, Exclusion for F039 and F037 Wastes, and Eastman Chemical Company –
Longview, Texas Exclusion for Wastewater Treatment Sludge, F001, F002, F003, and
F005, 40 CFR Part 261, Appendix DC, Table 1.
(Attachment 4 hereto)
The constituents of concern ("COC's") in Table A of the Adjusted Standard were
derived as prescribed by EPA in the "EPA RCRA Delisting Program Guidance Manual
for the Petitioner," March 23, 2000 ("Guidance Manual") and accepted by EPA in
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17

 
granting similar petitions for delisting.
See Guidance Manual, p. 3. Also see Hazardous
Waste Delisting Petition, Shell Oil Company — Deer Park Texas, Jan. 20, 2003, p.
(Attachment 5 hereto)
First, the leachate was tested for a broad list of constituents, including all of the
constituents in 35 Ill. Adm. Code 721, Appendix J, (40 CFR 261, Appendix IX). In
2005, BFI performed five additional sampling events which focused on any additional
constituents which were the basis of EPA's F039 listing, any additional constituents
contained in Table 1 — Maximum Concentration of Contaminants for the Toxicity
Characteristic, 35 Ill. Adm. Code 721.124(b), (40 CFR 261.24(b)), and the ignitability,
reactivity and corrosivity characteristics. This "initial list" is what Weaver Boos refers to
as the Comprehensive Constituent List for the Phase I Unit leachate provided in
Appendix D
to the
Technical Support Document.
It includes over 230 constituents.
Table A in the Adjusted Standard includes all of the constituents found in the
Phase I Unit leachate which have been detected at any time in fifteen sampling events
over the last nine years. The delisting levels for that "final list" of constituents in Table A
were derived respectively from the DRAS model, EPA published MCLs and toxicity
standards, and a site and constituent specific risk assessment.
The Adjusted Standard requires that the concentrations of these constituents in the
Phase I Unit leachate be less than or equal to the Table A delisting levels. The Adjusted
Standard also requires that the leachate not exhibit a hazardous characteristic, i.e.
ignitability, corrosivity, reactivity, or toxicity, as defined in 35 Ill. Adm. Code 721.121,
721.122, 721123 and 721.124, (40 CFR 261.121, 261.122, 261.123 and 261.124).
Printed On Recycled Paper
18

 
Consistent with similar EPA delistings, the Adjusted Standard requires that if a
representative sample is confirmed to exceed the delisting levels or exhibits a hazardous
characteristic (after excluding sampling or laboratory error), the leachate must be
managed and disposed of as a hazardous waste until such time as subsequent tests of
representative samples confirm compliance with the delisting levels.
See Shell Oil
Company and Eastman Chemical delistings in 40 CFR 261, Appendix IX, Table 1-
Wastes Excluded from Non-Specific Sources.
(Attachment
4
hereto)
The proposed Adjusted Standard requires that the Phase I Unit leachate be
transported and disposed of as an Illinois Special Waste pursuant to 35 Ill. Adm. Code
Part 809. This assures that the leachate will be tracked from the landfill to disposal by
way of a Special Waste manifest.
The Adjusted Standard allows the leachate to be transported for disposal at a
permitted waste water treatment facility subject to Clean Water Act discharge
requirements. This is consistent with the domestic sewer exemption in 35 Ill. Adm. Code
721.104 (40 CFR 261.4 (a)). See discussion in
Section 9.3.2 of the Technical Support
Document.
It is also consistent with the statutory exemption for certain F039 leachate
found in 35 Ill. Adm. Code 721.104(b)(15)(A)(iv) ( 40 CFR 261.(b)(15(A)(iv)). That
exemption exempts from the definition of hazardous waste certain leachate and gas
condensate from landfills where certain listed hazardous wastes were disposed of, on
certain conditions, including the condition that the waste stream is being transported for
treatment and disposal at an off-site facility which is subject to regulation under Section
307(b) or 402 of the Federal Clean Water Act.
Printed On Recycled Paper
19

 
Consistent with similar EPA delistings, the Adjusted Standard requires that a one-
time written notification be given to Illinois EPA, the applicable state regulatory agency,
60 days before commencing transportation of the delisted leachate.
See delisting
conditions stated for Shell Oil Company and Eastman Chemical multi-source leachate
delistings in 40 CFR 261, Appendix
D(
Table 1- Wastes Excluded from Non-Specific
Sources.
Attachment 4 hereto.
Unlike the federal delistings, the Adjusted Standard in
this case is limited to transportation and disposal within Illinois.
2.
Efforts Necessary to Achieve Proposed Standard
As demonstrated by the nine years of leachate data presented with this petition,
the quality of the Phase I Unit leachate has stabilized. The DRAS modeling results and
risk analysis presented in the
Technical Support Document
demonstrate that the
detected constituents will not pose a risk to health or the environment even at the highest
concentrations detected over the last nine years and even in a worst case release scenario.
Therefore, BFI does not anticipate any additional efforts will be required to achieve the
conditions imposed by the proposed adjusted standard.
3.
Cost Necessary to Achieve Proposed Standard
As indicated in Section E above, the cost of compliance with the proposed
Adjusted Standard is anticipated to be approximately $0.045 per gallon of leachate. This
is a cost savings of approximately $30,000 per 100,000 gallons when compared to the
current cost of compliance.
Printed On Recycled Paper
20

 
F.
Quantitative and Qualitative Environmental Impact of Compliance with
Existing Regulations vs Adjusted Standard
The treatment the leachate receives at the CID facility, over 100 miles away, is
not more protective of the environment than that which the leachate would be subject to
at a more local non-hazardous industrial waste water treatment facility. The CID facility
uses a biological treatment system to achieve its NPDES discharge limits. The IPC
facility uses a chemical treatment process and discharges to a POTW, at which the final
discharge is subject to NPDES discharge requirements.
The current long distance hauling of the Phase I Unit leachate is energy inefficient
and generates excess air pollution in the form of diesel emissions, including carbon
dioxide, nitrogen oxide, volatile organics, particulate, Hazardous Air Pollutants, and soot.
Based on simple mathematics, hauling the leachate over ten times further to CID
generates over 90% more emissions and uses 90% more fuel than hauling the leachate to
the IPC facility. It also results in an increased potential for highway accidents resulting in
releases to the environment.
G.
Justification for the proposed Adjusted Standard (35
Ill.
Adm.
104.406(h))
1. The
Phase I Unit leachate does not meet the criteria for which F039
was listed as hazardous. (35
Ill.
Adm. Code 720.122(a)(1))
Section 721.122(n) (40 CFR 260.22(n)) requires that a petitioner demonstrate that
a waste does not meet any of the criteria under which the waste was listed as hazardous
or acutely hazardous. The Phase I Unit leachate is considered "multi-source leachate"
covered under the F039 listing. F039 is listed with the code "T" which indicates that it
was listed as a hazardous waste based upon "toxicity." For a "T" waste, a delisting
Printed On Recycled Paper
21

 
petitioner must either demonstrate that the waste does not contain the hazardous
constituents that caused EPA to list the waste as hazardous, or, although containing one
or more of those constituents, it does not meet the listing criteria when considering the
listing factors in Section 721.111(a)(3)(A) through (K), (40 CFR 261.11(a)(3)(i) through
(xi)).
As previously discussed, BFI has provided an extensive database on this leachate
which includes nine years of testing, fifteen sampling events, and several thousand data
points. That database includes test results for all of the constituents which formed the
basis for which F039 was listed as a hazardous waste under 35 Ill. Code 721 (40 CFR
261). That testing demonstrates that the vast majority of those constituents have never
been detected.
For those constituents that were detected, BFI, as a first step, modeled the risk
posed by the leachate using the DRAS model specified in the
"EPA RCRA Delisting
Program--Guidance Manual for the Petitioner,"
incorporated by reference in Section
720.111(a). The DRAS model takes into account the Section 721.111(a)(3) factors,
including the concentration of the constituent in the waste, health-based standards and the
volume of waste that may be released in a plausible worst case scenario. In its most
recent delisting opinion, the Board confirmed that the DRAS is the preferred model to be
used in a delisting petition pursuant to Section 720.122.
See Petition of BP Products
North America, Inc. for RCRA Waste Delisting Under 35 Ill. Adm. Code 720.122, AS 07-
1 (Feb. 15, 2007 Opinion and Order p. 8).
BFI used conservative assumptions in the DRAS modeling. BFI assumed direct
land disposal of the leachate — assuming the possibility of an accidental release of an
Printed On Recycled Paper
22

 
entire tanker truck of the Phase I Unit leachate - despite the fact that the Adjusted
Standard requires that the leachate be disposed of at a permitted waste water treatment
facility where it will be treated before ultimate disposal. This is consistent with EPA's
position, cited in the Board's
BP Products Opinion and Order,
that land disposal is a
worst case assumption. Use of the entire tank volume is consistent with EPA's worst
case discharge planning volume for a tanker truck release, as stated in 40 CFR 112,
Appendix D.
The DRAS model generated "delisting levels" for each of the modeled
constituents. Comparing those "delisting levels" to the maximum concentration of each
of the constituents detected over the last nine years, all but four of the constituents were
consistently found in concentrations below the "delisting levels." For the four
constituents that exceeded the delisting levels, methylene chloride, trichloroethylene,
vinyl chloride, and 1,4-dioxane, BFI undertook additional analysis. That analysis is
discussed in detail in Section 9.2 of the
Technical Support Document.
2. Based
on the criteria specified in the "EPA RCRA Delisting Program-
-Guidance Manual for the Petitioner," incorporated by reference in Section
720.111(a), there is a reasonable basis to believe that factors (including
additional constituents) other than those for which F039 was listed could
cause the waste to be a hazardous waste, that such factors do not warrant
retaining the Phase
I
Unit leachate as a hazardous waste.
(35 Ill
Adm. Code
720.122(a)(2))
As discussed above, BFI's extensive database on the Phase I Unit leachate goes
well beyond the constituents which formed the basis of EPA's F039 listing. It includes
nine years of data for the entire Appendix IX list of hazardous constituents, as well as
supplemental sampling for any ignitability, reactivity, and corrosivity, and additional
toxicity characteristic constituents listed in Table 1 of 35 Ill. Adm. Code 721.124(b) (40
Printed On Recycled Paper
23

 
CFR 261.24(b)). There are 230 constituents in the Comprehensive Constituent List,
Appendix D to the Technical Support Document.
As noted in Section G.1 above, BFI modeled all of the detected constituents using
the DRAS model and found only four constituents which exceeded the DRAS "delisting
levels."
Based on the very comprehensive list of constituents, the many years of sampling
and many sampling events, and the conservative delisting levels reflected in the Adjusted
Standard, there is no other reasonable basis to believe that the Phase
I
Unit leachate
should be maintained as a hazardous waste.
3.
?
The Phase I Unit leachate is not hazardous waste by operation of
Subpart
C of 35 III.
Adm. Code 721, i.e. is not a hazardous waste by virtue of
exhibiting one of the hazardous characteristics specified in Subpart
C. (35 III.
Adm. Code 720.122(a)(2))
As discussed in detail in
Section 7.3.1 of the Technical Support Document,
test
data and generator knowledge demonstrate that the Phase
I
Unit leachate does not exhibit
any hazardous characteristic.
H.
?
Consistency with Federal Law (35 III. Adm. Code 104.406(i))
Federal law provides the regulatory framework for delisting this or any other
hazardous waste. The proposed Adjusted Standard meets the requirements prescribed in
35 Ill. Adm. Code 720.122 which are identical in substance to the requirements for
delisting a hazardous waste prescribed in 40 CFR 260.122.
Printed On Recycled Paper
24

 
Patricia . har
I.
Request for Hearing
(35 III.
Adm. Code 104.406(j))
BFI respectfully requests that a hearing be held in this matter pursuant to 35 Ill.
Adm. Code 104.422 to allow for a full review of the proposed Adjusted Standard and
the facts supporting this Petition.
J.
Supporting Documents
(35 III.
Adm. Code 104.406(k))
See the
Technical Support Document attached hereto as Attachment 1.
CONCLUSION
WHEREFORE, BFI requests that the Board grant an Adjusted Standard pursuant
to Section 28.1 of the Illinois Environmental Protection Act ("Act"), 415 ILCS 5/28.1,
delisting the leachate generated at the Phase Unit of the BFI Davis Junction Landfill
consistent with the conditions in the Adjusted Standard proposed in this Petition or such
other reasonable terms and conditions as the Board deems appropriate to provide the
relief requested. BFI further requests that the Board schedule a hearing in this matter to
allow full review of the proposed Adjusted Standard and the facts supporting this
petition.
Respectfully submitted,
BFI WASTE SYSTEMS OF NORTH AMERICA, INC.
By On of Its Attorneys
Patricia F. Sharkey
McGuireWoods LLP
77 West Wacker Drive, Suite 4100
Chicago, Illinois 60601
Telephone: 312/849-8100
Attorney Reg.: 6181113
Printed On Recycled Paper
25

 
Petition of BFI Waste Systems of North America, Inc.
Attachments
1.
Weaver Boos Technical Support Document, Petition to Delist Hazardous Waste,
November 21, 2007.
2.
MapQuest Route Map for route to CID Facility.
3. MapQuest Route Map for route to IPC Facility.
4.
Federal Delistings for Shell Oil Company and Eastman Chemical Company, 40 CFR 261,
Appendix IX, Table I.
5.
Hazardous Waste Delisting Petition, Shell Oil Company — Deer Park, Texas, January 20,
2003, p. 35.
Printed On Recycled
Paper

 
Exhibit 1

 
Attachment 1
Attachment 1, Weaver Boos Consultants' Support Document, including
the Signed Certification Statement, is contained in the attached Binders 1
and 2.
Printed On Recycled Paper

 
Exhibit 2

 
Sorry!
When printing directly from the browser your map may be incorrectly cropped. To print the
entire map, try clicking the
"Printer
-
Friendly"
link at the top of your results page.
At
tachment 2
Driving Directions from 8902 N Il Route 251, Davis Junction,
IL
to Calumet City,
IL
Page
1 of 3
An
AOL
Company,
iza 8902
N
II
Route 251
Davis Junction, IL 61020-9706, US
Total Est. Time:
2 hours, 3 minutes
la
Calumet
City, IL US
Total Est. Distance:
110.09 miles
Maneuvers
1:
Start out going NORTH on IL-251 N toward E SCOTT RD.
2:
Turn RIGHT onto BAXTER RD / CR-11.
3:
Merge onto 1-39 N / US-51 N via the ramp on the LEFT toward
ROCKFORD.
4: Merge onto
1-90 E toward CHICAGO (Portions toll).
5:
Keep LEFT to take 1-90 E via EXIT 59A toward INDIANA TOLL RD
(Portions toll) (Crossing into INDIANA).
6:
Take the CALUMET AVE / US-41 exit- EXIT 5.
7: Turn LEFT onto S CALUMET AVE / US-41.
8:
Turn RIGHT onto E CHICAGO ST / IN-312. Continue to follow IN-312.
9:
Turn LEFT onto S HOHMAN AVE.
10:
Turn RIGHT onto E SIBLEY ST (Crossing into ILLINOIS).
11: Turn LEFT onto S STATE LINE AVE / STATE LINE RD.
12: Turn RIGHT onto E 154TH ST / PULASKI RD.
Ca
13:
End at
Calumet City, IL US
Total Est. Time:
2 hours, 3 minutes?
Total Est. Distance:
110.09 miles
Distance
2.2 miles
2.7 miles
7.0 miles
83.1 miles
12.1 miles
0.2 miles
0.5 miles
0.4 miles
0.6 miles
0.2 miles
0.3 miles
0.2 miles
http://www.mapquest.com/directions/main.adp?go=1&do=nw&rmm=1&2si=navt&un=m...
10/7/2007

 
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Driving Directions from 8902 N Il Route 251, Davis Junction, IL to Calumet City, IL
?
Page 2 of 3
Sorry! When printing directly from the browser your map may be incorrectly cropped. To print the
entire map, try clicking the "Printer-Friendly" link at the top of your results page.
All rights reserved. Use Subject
to License/Copyrght
These
directions are informational only. No represen ation is made or warranty given as to their content, road conditions or
route usability or expeditiousness. User assumes all isk of use. MapQuest and its suppliers assume no responsibility for any
loss or delay resulting from such use.
http://www.mapquest.com/directions/main.adp?go=l&clo=nw&rmm=1&2si=navt&un=m... 10/7/2007

 
Exhibit 3

 
Driving Directions from
8902
N
II
Route
251,
Davis Junction,
IL
to
4430
Boeing Dr, Roc... Page
1 of 3
Sorry!
When printing directly from the browser your map may be incorrectly cropped. To print the
entire map, try clicking the "Printer-Friendly"
link at the top of your results page.
AOL
Compa ny
=2
8902
N II
Route 251
Davis Junction, IL 61020-9706, US
Total Est. Time:
11 minutes
Attachment
3
gm
4430 Boeing Dr
Rockford, IL 61109-2931, US
Total Est. Distance:
6.55 miles
Maneuvers
1: Start out
going NORTH on IL-251 N toward E SCOTT RD.
2:
Turn LEFT onto AIRPORT DR.
3:
Turn RIGHT onto KISHWAUKEE ST.
4: Turn LEFT onto BOEING DR.
Distance
5.3 miles
0.7 miles
0.3 miles
<0.1 miles
e
Ca
0
5: End at
4430 Boeing Dr
Rockford, IL 61109
-
2931, US
Total Est. Time:
11 minutes?
Total
Est. Distance:
6.55 miles
http://www.mapquest.com/directions/main.adp?go—
l&do—nw&rmm=1&un=m8cc1
=EN&q...
10/7/2007

 
Sorry! When printing directly from the browser your map may be incorrectly cropped. To print the
entire map, try clicking the "Printer-Friendly" link at the top of your results page.
Driving Directions from 8902 N 11 Route 251, Davis Junction, IL to 4430 Boeing Dr, Roc... Page 2 of 3
.
MAPCN E
?
2007 MapOui
All rights reserved. Use Subject to License/Copyright
These directions are informational only. No representation is made or warranty given as to their content, road conditions or
route usability or expeditiousness. User assumes all risk of use. MapQuest and its suppliers assume no responsibility for any
loss or delay resulting from such use.
http://www.mapquest.com/directions/main.adp?go=
l&do=nw&rmm=l&un=m&c1=EN&q
...
10/7/2007

 
Exhibit 4

 
ATTACHMENT 4
40 C.F.R. Pt. 261., App. IX
Code of Federal Regulations Currentness
Title 40. Protection of Environment
Chapter I. Environmental Protection Agency (Refs Annos),
Subchapter I. Solid Wastes
NAPart 261. Identification and Listing of Hazardous Waste 'Refs
& Annos)
‘tiAppendices to Part 261
*Appendix IX to Part 261--Wastes Excluded Under §g 260.20 and 260.22
TABLE 1-WASTES EXCLUDED FROM NON-SPECIFIC SOURCES
Facility
?
Address?
Waste description
Shell Oil
Company ?
Deer Park, TX North Pond Sludge (EPA Hazardous Waste
No. F037) generated one time at a
volume of 15,000 cubic yards August
23, 2005 and disposed in a Subtitle
D landfill. This is a one time
exclusion and applies to 15,000
cubic yards of North Pond Sludge.
(1) Reopener:
(A)
If, anytime after disposal of the
delisted waste,
Shell
possesses or
is otherwise made aware of any
environmental data (including but
not limited to leachate data or
ground water monitoring data) or any
other data relevant to the delisted
waste indicating that any
constituent identified for the
delisting verification testing is at
level higher than the delisting
level allowed by the Division
Director in granting the petition,
then the facility must report the
data, in writing, to the Division
Director within 10 days of first
possessing or being made aware of
that data.
(B)
If Shell
fails to submit the
information described in paragraph
(A) or if any other information is
received from any source, the
Division Director will make a
preliminary determination as to
whether the reported information
requires EPA action to protect human
health or the environment. Further
action may include suspending, or
revoking the exclusion, or other
appropriate response necessary to
protect human health and the
environment.
(C)
If the Division Director

 
determines that the reported
information does require EPA action,
the Division Director will notify
the facility in writing of the
actions the Division Director
believes are necessary to protect
human health and the environment.
The notice shall include a statement
of the proposed action and a
statement providing the facility
with an opportunity to present
information as to why the proposed
EPA action is not necessary. The
facility shall have 10 days from the
date of the Division Director's
notice to present such information.
(D)
Following the receipt of
information from the facility
described in paragraph (C) or if no
information is presented under
paragraph (C), the Division Director
will issue a final written
determination describing the actions
that are necessary to protect human
health or the environment. Any
required action described in the
Division Director's determination
shall become effective immediately,
unless the Division Director
provides otherwise.
(2) Notification Requirements: Shell
must do the following before
transporting the delisted waste:
Failure to provide this notification
will result in a violation of the
delisting petition and a possible
revocation of the decision.
(A)
Provide a one-time written
notification to any state regulatory
agency to which or through which
they will transport the delisted
waste described above for disposal,
60 days before beginning such
activities.
(B)
Update the one-time written
notification, if they ship the
delisted waste to a different
disposal facility.
(C)
Failure to provide this
notification will result in a
violation of the delisting variance
and a possible revocation of the
decision.
Shell Oil Company
?
Deer Park, TX Multi-source landfill leachate (EPA
Hazardous Waste No. F039) generated
at a maximum annual rate of 3.36
million gallons (16,619 cu. yards)
per calendar year after August 23,
2005 and disposed in accordance with
the TPDES permit.
The delisting levels set do not
relieve Shell Oil Company of its
duty to comply with the limits set

 
in its TPDES permit. For the
exclusion to be valid,
Shell
Oil
Company must implement a
verification testing program that
meets the following paragraphs:
(1)
Delisting Levels: All total
concentrations for those
constituents must not exceed the
following levels (mg/1). The
petitioner must analyze the aqueous
waste on a total basis to measure
constituents in the multi-source
landfill leachate.
Multi-source landfill leachate (i)
Inorganic Constituents
Antimony-0.0204; Arsenic-0.385;
Barium-2.92; Copper-418.00;
Chromium-5.0; Cobalt-2.25;
Nickel-1.13; Selenium-0.0863;
Thallium-0.005; Vanadium-0.838
(ii) Organic Constituents
Acetone-1.46; Acetophenone-1.58;
Benzene-0.0222; p-Cresol-0.0788;
Bis(2-ethylhexyl)phthlate-15800.00;
Dichloroethane, 1,2-0.0803;
Ethylbenzene-4.51; Fluorene-1.87;
Napthalene-1.05; Phenol-9.46;
Phenanthrene-1.36; Pyridine-0.0146;
2,3,7,8-TCDD equivalents as
TEQ-0.0000926; Toluene-4.43;
Trichloropropane-0.000574; Xylenes
(total)-97.60
(2)
Waste Management:
(A)
Shell
Oil
Company must manage as
hazardous all multi-source landfill
leachate generated, until it has
completed initial verification
testing described in paragraph
(3)(A) and (B), as appropriate, and
valid analyses show that paragraph
(1) is satisfied.
(B)
Levels of constituents measured in
the samples of the multi-source
landfill leachate that do not exceed
the levels set forth in paragraph
(1) are non-hazardous.
Shell
Oil
Company can manage and dispose of
the non-hazardous multi-source
landfill leachate according to all
applicable solid waste regulations.
(C)
If constituent levels in a sample
exceed any of the delisting levels
set in paragraph (1),
Shell
Oil
Company can collect one additional
sample and perform expedited
analyses to verify if the
constituent exceeds the delisting
level. If this sample confirms the
exceedance, Shell
Oil
Company must,
from that point forward, treat the
waste as hazardous until it is
demonstrated that the waste again
meets the levels in paragraph (1).

 
(D)
If the facility has not treated
the waste, Shell Oil Company must
manage and dispose of the waste
generated under Subtitle C of RCRA
from the time that it becomes aware
of any exceedance.
(E)
Upon completion of the
Verification Testing described in
paragraph 3(A) and (B) as
appropriate and the transmittal of
the results to EPA, and if the
testing results meet the
requirements of paragraph (1), Shell
Oil Company may proceed to manage
its multi-source landfill leachate
as non-hazardous waste. If
Subsequent Verification Testing
indicates an exceedance of the
delisting levels in paragraph (1),
Shell Oil Company must manage the
multi-source landfill leachate as a
hazardous waste until two
consecutive quarterly testing
samples show levels below the
delisting levels in Table I.
(3) Verification Testing Requirements:
Shell Oil Company must perform
sample collection and analyses,
including quality control
procedures, using appropriate
methods. As applicable to the
method-defined parameters of
concern, analyses requiring the use
of SW-846 methods incorporated by
reference in 40 CFR 260.11 must be
used without substitution. As
applicable, the SW-846 methods might
include Methods 0010, 0011, 0020,
0023A, 0030, 0031, 0040, 0050, 0051,
0060, 0061, 1010A, 1020B, 1110A,
13108, 1311, 1312, 1320, 1330A,
9010C, 9012B, 9040C, 9045D, 9060A,
9070A (uses EPA Method 1664, Rev.
A), 9071B, and 90958. Methods used
must meet Performance Based
Measurement System Criteria in which
the Data Quality Objectives
demonstrate that representative
samples of the Shell-Deer Park
multi-source landfill leachate are
collected and meet the delisting
levels in paragraph (1).
(A) Initial Verification Testing:
After EPA grants the final
exclusion, Shell Oil Company must do
the following:
(i)
Within 60 days of this exclusions
becoming final, collect four
samples, before disposal, of the
multi-source landfill leachate.
(ii)
The samples are to be analyzed
and compared against the delisting
levels in paragraph (1).

 
(iii)
Within sixty (60) days after
this exclusion becomes final,
Shell
Oil Company will report initial
verification analytical test data
for the multi-source landfill
leachate, including analytical
quality control information for the
first thirty (30) days of operation
after this exclusion becomes final.
If levels of constituents measured
in the samples of the multi-source
landfill leachate that do not exceed
the levels set forth in paragraph
(1) are also non-hazardous in two
consecutive quarters after the first
thirty (30) days of operation after
this exclusion become effective,
Shell
Oil Company can manage and
dispose of the multi-source landfill
leachate according to all applicable
solid waste regulations.
(B)
Subsequent Verification Testing:
Following written notification by
EPA,
Shell
Oil Company may
substitute the testing conditions in
(3)(E) for (3)(A).
Shell
Oil Company
must continue to monitor operating
conditions, and analyze one
representative sample of the
multi-source landfill leachate for
each quarter of operation during the
first year of waste generation. The
sample must represent the waste
generated during the quarter. After
the first year of analytical
sampling verification sampling can
be performed on a single annual
sample of the multi-source landfill
leachate. The results are to be
compared to the delisting levels in
paragraph (I).
(C)
Termination of Testing:
(i)
After the first year of quarterly
testing, if the delisting levels in
paragraph (1) are being met,
Shell
Oil Company may then request that
EPA not require quarterly testing.
After EPA notifies
Shell
Oil Company
in writing, the company may end
quarterly testing.
(ii)
Following cancellation of the
quarterly testing,
Shell
Oil Company
must continue to test a
representative sample for all
constituents listed in paragraph (1)
annually.
(4) Changes in Operating Conditions:
If
Shell
Oil Company significantly
changes the process described in its
petition or starts any processes
that generate(s) the waste that may
or could significantly affect the
composition or type of waste

 
generated as established under
paragraph (1) (by illustration, but
not limitation, changes in equipment
or operating conditions of the
treatment process), it must notify
EPA in writing; it may no longer
handle the wastes generated from the
new process as nonhazardous until
the wastes meet the delisting levels
set in paragraph (1) and it has
received written approval to do so
from EPA.
(5) Data Submittals: Shell Oil Company
must submit the information
described below. If Shell Oil
Company fails to submit the required
data within the specified time or
maintain the required records
on-site for the specified time, EPA,
at its discretion, will consider
this sufficient basis to reopen the
exclusion as described in paragraph
6. Shell Oil Company must:
(A)
Submit the data obtained through
paragraph 3 to the Section Chief,
Region 6 Corrective Action and Waste
Minimization Section, EPA, 1445 Ross
Avenue, Dallas, Texas 75202-2733,
Mail Code, (6PD-C) within the time
specified.
(B)
Compile records of operating
conditions and analytical data from
paragraph (3), summarized, and
maintained on-site for a minimum of
five years.
(C)
Furnish these records and data
when EPA or the state of Texas
request them for inspection.
(D)
Send along with all data a signed
copy of the following certification
statement, to attest to the truth
and accuracy of the data submitted:
Under civil and criminal penalty of
law for the making or submission of
false or fraudulent statements or
representations (pursuant to the
applicable provisions of the Federal
Code, which include, but may not be
limited to, 18 U.S.C. 1001 and 42
U.S.C. 6928), I certify that the
information contained in or
accompanying this document is true,
accurate and complete.
As to the (those) identified
section(s) of this document for
which I cannot personally verify its
(their) truth and accuracy, I
certify as the company official
having supervisory responsibility
for the persons who, acting under my
direct instructions, made the
verification that this information
is true, accurate and complete.

 
If any of this information is
determined by EPA in its sole
discretion to be false, inaccurate
or incomplete, and upon conveyance
of this fact to the company, I
recognize and agree that this
exclusion of waste will be void as
if it never had effect or to the
extent directed by EPA and that the
company will be liable for any
actions taken in contravention of
the company's RCRA and CERCLA
obligations premised upon the
company's reliance on the void
exclusion.
(6) Reopener:
(A)
If, anytime after disposal of the
delisted waste, Shell Oil Company
possesses or is otherwise made aware
of any environmental data (including
but not limited to leachate data or
groundwater monitoring data) or any
other data relevant to the delisted
waste indicating that any
constituent identified for the
delisting verification testing is at
a level higher than the delisting
level allowed by the Division
Director in granting the petition,
then the facility must report the
data, in writing, to the Division
Director within 10 days of first
possessing or being made aware of
that data.
(B)
If the annual testing of the waste
does not meet the delisting
requirements in paragraph 1, Shell
Oil Company must report the data, in
writing, to the Division Director
within 10 days of first possessing
or being made aware of that data.
(C)
If Shell Oil Company fails to
submit the information described in
paragraphs (5), (6) (A) or (6) (B) or
if any other information is received
from any source, the Division
Director will make a preliminary
determination as to whether the
reported information requires EPA
action to protect human health
and/or the environment. Further
action may include suspending, or
revoking the exclusion, or other
appropriate response necessary to
protect human health and the
environment.
(0) If the Division Director
determines that the reported
information does require action, he
will notify the facility in writing
of the actions the Division Director
believes are necessary to protect
human health and the environment.

 
The notice shall include a statement
of the proposed action and a
statement providing the facility
with an opportunity to present
information as to why the proposed
action by EPA is not necessary. The
facility shall have 10 days from the
date of the Division Director's
notice to present such information.
(E) Following the receipt of
information from the facility
described in paragraph (6)(D) or if
no information is presented under
paragraph (6)(D), the Division
Director will issue a final written
determination describing the actions
that are necessary to protect human
health and/or the environment. Any
required action described in the
Division Director's determination
shall become effective immediately,
unless the Division Director
provides otherwise.
(7) Notification Requirements: Shell
Oil Company must do the following
before transporting the delisted
waste. Failure to provide this
notification will result in a
violation of the delisting petition
and a possible revocation of the
decision.
(A)
Provide a one-time written
notification to any state regulatory
agency to which or through which it
will transport the delisted waste
described above for disposal, 60
days before beginning such
activities.
(B)
Update the one-time written
notification if it ships the
delisted waste into a different
disposal facility.
(C)
Failure to provide this
notification will result in a
violation of the delisting exclusion
and a possible revocation of the
decision.
Eastman
Chemical
?
Longview,?
Wastewater treatment sludge, (at a maximum
Company.
? Texas?
generation of 82,100 cubic yards per calendar
year) generated by
Eastman
(EPA Hazardous
Waste Nos. F001, F002, F003, FOOS generated at
Eastman
when disposed of in a Subtitle
D
landfill.
Eastman
must implement a testing program that
meets the following conditions for the
exclusion to be valid:
(1) Delisting Levels: All concentrations for the
following constituents must not exceed the
following levels (mg/1). For the wastewater
treatment sludge constituents must be measured

 
in the waste leachate by the method specified
in 40 CFR 261.24. Wastewater treatment sludge:
(i)
Inorganic Constituents: Antimony-0.0515;
Barium-7.30; Cobalt-2.25; Chromium-5.0;
Lead-5.0; Mercury-0.0015; Nickel-2.83;
Selenium-0.22; Silver-0.384; Vanadium-2.11;
Zinc-28.0
(ii)
Organic Constituents: Acenaphthene-1.25;
Acetone--7.13;
bis(2-ethylhexylphthalate--0.28;
2-butanone--42.8; Chloroform--0.0099;
Fluorene--0.55; Methanol-35.7; Methylene
Chloride--0.486; naphthalene-0.0321.
(2)
Waste Holding and Handling: If the
concentrations of the sludge exceed the levels
provided in Condition 1, then the sludge must
be treated in the Fluidized Bed Incinerator
(FBI) and meet the requirements of that
September 25, 1996 delisting exclusion to be
non-hazardous (as FBI ash). If the sludge
meets the delisting levels provided in
Condition 1, then it's non-hazardous (as
sludge). If the waste water treatment sludge
is not managed in the manner above,
Eastman
must manage it in accordance with applicable
RCRA Subtitle C requirements. If the levels of
constituents measured in the samples of the
waste water treatment sludge do not exceed the
levels set forth in Condition (1), then the
waste is nonhazardous and may be managed and
disposed of in accordance with all applicable
solid waste regulations. During the
verification period,
Eastman
must manage the
waste in the FBI incinerator prior to
disposal.
(3)
Verification Testing Requirements:
Eastman
must perform sample collection and analyses,
including quality control procedures, using
appropriate methods. As applicable to the
method-defined parameters of concern, analyses
requiring the use of SW-846 methods
incorporated by reference in 40 CFR 260.11
must be used without substitution. As
applicable, the SW-846 methods might include
Methods 0010, 0011, 0020, 0023A, 0030, 0031,
0040, 0050, 0051, 0060, 0061, 1010A, 1020B,
1110A, 1310B, 1311, 1312, 1320, 1330A, 9010C,
9012B, 9040C, 9045D, 9060A, 9070A (uses EPA
Method 1664, Rev. A), 9071B, and 9095B. After
completion of the initial verification period,
Eastman
may replace the testing required in
Condition (3)(A) with the testing required in
Condition (3)(B).
Eastman
must continue to
test as specified in Condition (3)(A) until
and unless notified by EPA in writing that
testing in Condition (3)(A) may be replaced by
Condition (3)(B).
(A) Initial Verification Testing: At quarterly
intervals for one year after the final
exclusion
is granted,
Eastman
must collect and
analyze composites of the wastewater treatment
sludge for constituents listed in Condition
(1).

 
(B)
Subsequent Verification Testing: Following
termination of the quarterly testing,
Eastman
must continue to test a representative
(C) 2007 Thomson/West. No Claim to Orig. US Gov. Works.
Next Part»
composite sample for all constituents listed
in Condition (1) on an annual basis (no later
than twelve months after the final exclusion).
(4)
Changes in Operating Conditions. If
Eastman
significantly changes the process which
generate(s) the waste(s) and which may or
could affect the composition or type of
waste(s) generated as established under
Condition (1) (by illustration, but not
limitation, change in equipment or operating
conditions of the treatment process or
generation of volumes in excess 82,100 cubic
yards of waste annually),
Eastman
must (A)
notify the EPA in writing of the change and
(B)
may no longer handle or manage the waste
generated from the new process as nonhazardous
until
Eastman
has demonstrated through testing
the waste meets the delisting levels set in
Condition (1) and (C)
Eastman
has received
written approval to begin managing the wastes
as non-hazardous from EPA.
(5) Data Submittals.
Eastman
must submit or
maintain, as applicable, the information
described below. If
Eastman
fails to submit
the required data within the specified time or
maintain the required records on-site for the
specified time, EPA, at its discretion, will
consider this sufficient basis to reopen the
exclusion as described in Condition (6).
Eastman
must:
(A) Submit the data obtained through Condition
(3) to Mr. William Gallagher, Chief, Region 6
Delisting Program, EPA, 1445 Ross Avenue,
Dallas, Texas 75202-2733, Mail Code, (6PD-O)
within the time specified.
(B)
Compile records of operating conditions and
analytical data from Condition (3),
summarized, and maintained on-site for a
minimum of five years.
(C)
Furnish these records and data when EPA or
the State of Texas request them for
inspection.
(D)
Send along with all data a signed copy of
the following certification statement, to
attest to the truth and accuracy of the data
submitted:
(i) Under civil and criminal penalty of law for
the making or submission of false or
fraudulent statements or representations
(pursuant to the applicable provisions of the
Federal Code, which include, but may not be
limited to, 18 U.S.C. 1001 and 42 U.S.C.
6928), I certify that the information
contained in or accompanying this document is

 
true, accurate and complete.
(ii)
As to the (those) identified section(s) of
this document for which I cannot personally
verify its (their) truth and accuracy, I
certify as the company official having
supervisory responsibility for the persons
who, acting under my direct instructions, made
the verification that this information is
true, accurate and complete.
(iii)
If any of this information is determined
by EPA in its sole discretion to be false,
inaccurate or incomplete, and upon conveyance
of this fact to the company, I recognize and
agree that this exclusion of waste will be
void as if it never had effect or to the
extent directed by EPA and that the company
will be liable for any actions taken in
contravention of the company's RCRA and CERCLA
obligations premised upon the company's
reliance on the void exclusion.
(6) Reopener Language:
(A)
If, anytime after disposal of the delisted
waste,
Eastman
possesses or is otherwise made
aware of any environmental data (including but
not limited to leachate data or groundwater
monitoring data) or any other data relevant to
the delisted waste indicating that any
constituent identified for the delisting
verification testing is at level higher than
the delisting level allowed by the Regional
Administrator or his delegate in granting the
petition, then the facility must report the
data, in writing, to the Regional
Administrator or his delegate within 10 days
of first possessing or being made aware of
that data.
(B)
If the annual testing of the waste does not
meet the delisting requirements in Condition
(1),
Eastman
must report the data, in writing,
to the Regional Administrator or his delegate
within 10 days of first possessing or being
made aware of that data.
(C)
If
Eastman
fails to submit the information
described in Conditions (5), (6)(A) or (6)(B)
or if any other information is received from
any source, the Regional Administrator or his
delegate will make a preliminary determination
as to whether the reported information
requires Agency action to protect human health
or the environment. Further action may include
suspending, or revoking the exclusion, or
other appropriate response necessary to
protect human health and the environment.
(D)
If the Regional Administrator or his
delegate determines that the reported
information does require Agency action, the
Regional Administrator or his delegate will
notify the facility in writing of the actions
the Regional Administrator or his delegate
believes are necessary to protect human health
and the environment. The notice shall include
a statement of the proposed action and a
statement providing the facility with an

 
opportunity to present information as to why
the proposed Agency action is not necessary.
The facility shall have 10 days from the date
of the Regional Administrator or his
delegate's notice to present such information.
(E) Following the receipt of information from
the facility described in Condition (6)(D) or
(if no information is presented under
Condition (6)(D)) the initial receipt of
information described in Conditions (5),
(6)(A) or (6)(B), the Regional Administrator
or his delegate will issue a final written
determination describing the Agency actions
that are necessary to protect human health or
the environment. Any required action described
in the Regional Administrator or his
delegate's determination shall become
effective immediately, unless the Regional
Administrator or his delegate provides
otherwise.
(7) Notification Requirements. Eastman must do
following before transporting the delisted
waste off-site: Failure to provide this
notification will result in a violation of the
delisting petition and a possible revocation
of the exclusion.
(A)
Provide a one-time written notification to
any State Regulatory Agency to which or
through which they will transport the delisted
waste described above for disposal, 60 days
before beginning such activities.
(B)
Update the one-time written notification if
they ship the delisted waste into a different
disposal facility.

 
Exhibit 5

 
Attachment 5
Hazardous Waste
Delisting
Petition
Shell Oil Company
Deer Park, Texas
January 20, 2003
Volume 1 of 2

 
Shell Deer Park Refilling Company
A
Division of Shell
Oil Products Company LLC
P. 0. Box 100
Deer Park, TX 77536
January 21, 2003
CERTIFIED MAIL - RETURN RECEIPT REQUESTED
#7002 0860 0005 5019 4724
Mr. Damn Swartz-Larson
Chief OK/TX RCRA Permits Section
U.S. Environmental Protection Agency
Multimedia Planning & Permitting Division (6PD-O)
1445 Ross Avenue, Suite 1200
Dallas, Texas 75202-2733
Subject?
Delisting Petition for the MTR Landfill Leachate
EPA I.D. TXD067285973
Shell Oil Company
Deer Park, Texas
Dear Mr. Swartz-Larson:
Shell Deer Park Refining Company, on behalf of Shell Oil Company (Shell), is pleased to
submit one hard copy and one electronic copy of the Delisting Petition for the MTR Landfill
Leachate. This petition is submitted in accordance with Region 6 RCRA Delisting Guidance
Manual for the Petitioner. It is Shell's understanding that the EPA will acknowledge receipt of this.
petition by letter within five (5) days of receipt of this petition. Shell will, within seven (7) days of
receipt of the EPA's letter, submit a public notice to the local newspaper regarding the submittal of
the delisting petition to the EPA and will provide a copy -to all persons on our facility mailing list.
Shell will also send the EPA verification of this action (to be inserted in
Appendix B
of the
Delisting Petition) within two (2) days of the publication of the public notice in the newspaper.

 
We are sending the Texas Commission on Environmental Quality one copy of the
Delisting Petition and will have one copy available in the Deer Park public library for public
viewing. Please do not hesitate to contact Joe Phillips at (713) 246-1229 if you have any
questions or concerns with this submittal.
Sincerely,
Glenn E. Giblet
Aid
Manager, Environmental & Compliance Assurance
Deer Park Refining Services
Agent for Shell Deer Park Refining Company
Enclosures
cc:
CERTIFIED MAIL - RETURN RECEIPT REQUESTED
#7002 0860 0005 5019 4717
Registration and Reporting Section, MC-129
Texas Commission on Environmental Quality
P.O. Box 13087
Austin, Texas 78711-3087

 
HAZARDOUS WASTE DELISTING PETITION
FOR
SHELL OIL COMPANY
DEER PARK, TEXAS
VOLUME 1 OF
2
JANUARY
20, 2003
Prepared by:
Elizabeth Arceneaux, P.E., DEE
113 N. Johnson
San Marcos, Texas 78666
(512) 353-4720

 
TABLE OF CONTENTS
1.0
INTRODUCTION
1
1.1
OBJECTIVES
1
2.0
ADMINISTRATIVE INFORMATION SUMMARY
2
2.1
NAME AND ADDRESS OF PETITIONER
2
2.2
FACILITY CONTACT INFORMATION
2
2.3
LOCATION OF PETITIONED WASTE
2
2.4
DESCRIPTION OF PROPOSED ACTION
2
'2.5
STATEMENT OF INTEREST IN PROPOSED ACTION
4
2.6
JUSTIFICATION FOR DELISTING
4
2.7
CERTIFICATION STATEMENT
5
2.8
PUBLICATION OF NOTICE
5
3.0
WASTE AND WASTE MANAGEMENT HISTORY INFORMATION
6
3.1
DESCRIPTION OF PETITIONED WASTE
6
3.2
HISTORY OF WASTE GENERATION
6
3.3
WASTE MANAGEMENT HISTORY
8
4.0
PROCESS AND WASTE MANAGEMENT HISTORY INFORMATION
10
4.1
GENERAL OPERATIONS AT THE GENERATING FACILITY
10
4.2
OVERVIEW OF CONTRIBUTING MANUFACTURING
PROCESSES
10
4.3
LANDFILL OPERATION AND LEACHATE COLLECTION
4.4
DESCRIPTION
SYSTEM OF
WASTE MANAGEMENT UNITS
5.0
ANALYTICAL
4.5
PROCESS
PLAN
MATERIALS
DEVELOPMENTAND
WASTE
VOLUMES
35
5.1
CONSTITUENTS FORMING BASIS OF LISTING
35
19
?
24
29
005-01 rpt.doc
Page i

 
6.0
WASTE
5.2
?
SELECTION
SAMPLING
OF
INFORMATIONANALYTE
LIST
?
?
35
42
6.1
SAMPLING PERSONNEL INFORMATION
?
42
6.2
SAMPLING STRATEGY
?
42
6.3
SAMPLE COLLECTION AND IDENTIFICATION
?
42
6.4
SAMPLE PRESERVATION AND HANDLING
?
43
6.5
SAMPLING
DOCUMENTATION ?
45
6.6
SAMPLE CUSTODY
?
45
6.7
QUALITY ASSURANCE/QUALITY CONTROL PROCEDURES
?
46
6.8
STATEMENT OF REPRESENTATIVENESS OF SAMPLES
?
46
7.0
WASTE ANALYSIS INFORMATION
?
47
7.1
ANALYTICAL LABORATORY INFORMATION
?
47
7.2
SUMMARY OF ANALYTICAL RESULTS
?
47
8.0
DATA EVALUATION USING EPA DRAS ?
59
8.1
INPUT VALUES
?
59
8.2
DELISTING LEVELS
?
60
8.3
CUMULATIVE RISK ASSESSMENT
?
60
8.4
SUMMARY
?
60
APPENDICES
A?
Quality Assurance Report
B
Affidavit of Publication for Petition Submittal
C?
Field Logs and Laboratory Reports
D
Laboratory
Personnel Qualifications
E
Calculation of Dioxin TEQs
F?
EPA
DRAS Output Files
005-0 I rpt.doc
?
Page ii

 
I
1.0 INTRODUCTION
Elizabeth Arceneaux, P.E. was retained by Shell Oil Company in Deer Park, Texas (Shell) to
prepare a Hazardous Waste Delisting Petition (HWDP) for one waste stream currently
generated at the facility. This HWDP was developed in accordance with the EPA Region 6
Hazardous Waste Delisting Program requirements.
1.1 OBJECTIVES
The objective of this HWDP is to provide documentation necessary for EPA to use in
. determining eligibility for delisting the petitioned waste. This petition contains information
specified by EPA's guidance document titled:
Region' 6 RCRA Delisting Program Guidance
Manual for the Petitioner.
This information was collected from Shell documentation and
from data collected as a result of implementation of the Sampling and Analysis Plan (SAP)
developed for the facility and approved by EPA on May 31, 2002.
005-01 rptdoe
Page 1

 
2.0
ADMINISTRATIVE INFORMATION SUMMARY
2.1
NAME AND ADDRESS OF PETITIONER
The complete name and address of the facility submitting this petition is as follows:
Mailing Address
Site Address
Shell Oil Company
Shell Oil Company
P.O. Box 100
5900 Hwy 225 East
Deer Park, Texas 77536-0100
Deer Park, Texas 77536
EPA Identification Number: TXD067285973
A site location map for the facility is presented as
Figure 2-1.
2.2
FACILITY CONTACT INFORMATION
The following individual should be contacted for additional information relating to this
petition:
Mr. Joe Phillips
Environmental Specialist
Shell Oil Company
P.O. Box 100
Deer Park, Texas 77536-0100
Phone: (713) 246-1229
2.3
LOCATION OF PETITIONED WASTE
Shell Oil Company
5900 Hwy 225 East
Deer Park, Texas 77536
2.4
DESCRIPTION OF PROPOSED ACTION
Shell operates a refinery and chemical-manufacturing complex in Deer Park, Texas. Products
manufactured include gasolines, fuel oils, lubricants, base chemicals, specialty chemicals and
sulfur. Facilities include refinery and chemical process units, feed/intermediate product
storage tanks, dock/rail/truck shipping facilities and maintenance
005-01rpt.doc
Page 2

 
1:100 000-scale
metric
Produced by the United States Geological Survey
topographic map
GATE
2002
w.O.NO.?
005-01
Figure 2-1
Site Location Map
Shell Oil Company
Deer Park, Texas

 
facilities. Shell generates hazardous and nonhazardous industrial solid wastes as a result of
refinery and chemical processes, wastewater treatment, refinery/chemical plant feed, product
storage and distribution.
Some of the hazardous and nonhazardous solid wastes are disposed of in an onsite, permitted
hazardous waste landfill (MTR Landfill — Site 104). Leachate from this landfill requires
offsite disposal as an F039 (multisource leachate) listed waste. However, analytical data
collected monthly for this aqueous stream shows that it is not a characteristic waste and
contains little to no detectable concentrations of organic constituents. Therefore, Shell is
interested in seeking a conditional exclusion for the landfill leachate in accordance with
§40CFR260.20, §260.22 and "EPA Region 6 RCRA Delisting Program Guidance Manual for
the Petitioner."
2.5 STATEMENT OF INTEREST
IN
PROPOSED ACTION
Based on comprehensive chemical analyses performed on samples collected, this waste does
not exhibit the characteristics of a hazardous waste and does not meet the criteria for which it
was listed.
Once delisted Shell plans to treat the leachate in the refinery's North Effluent Treater (NET)
authorized under the National Pollutant Discharge Elimination Systems (NPEDS) program.
The leachate will be treated onsite and discharged rather than sent offsite for disposal at a
permitted commercial facility.
2.6 JUSTIFICATION FOR DELISTING
Shell has performed extensive testing of the petitioned waste stream by undertaking a
comprehensive sampling and analysis program. EPA was involved in developing the SAP
and approved its use on May 31, 2002. Eight samples were collected of the waste (four
primary and four secondary) and analyzed for a complete suite of parameters specified by the
SAP. The waste was not found to be characteristically hazardous. A copy of the Quality
Assurance Report for this project is included as Appendix A.
Using Region 6 Delisting Risk Assessment Software (DRAS), the analytical results also
show that the waste does not contain levels of hazardous or nonhazardous constituents that
would pose a significant risk to human health or the environment. The DRAS program
evaluated a scenario assuming that the leachate were treated in a surface impoundment such
as the NET onsite.
005-01rpt.doc
Page 4

 
2.7
CERTIFICATION STATEMENT
I certify under penalty of law that I have personally examined and am familiar with the
information submitted in this demonstration and all attached documents, and that, based on
my inquiry of those individuals immediately responsible for obtaining information, I believe
that the submitted information is true, accurate and complete. I am aware that there are
significant penalties for submitting false information, including possibility of a fine and
imprisonment.
Signed,
Dean Eshelman
Plant Manager
Shell Chemical Company, Deer Park, Texas
Tim Hake
President and CEO
Shell Deer Park Refining Company
Notary et{
geA-ti
2.8
PUBLICATION OF NOTICE
MADONNA V. PORTER
MY COMMISSION EXPIRES
October 27, 2005
A copy of the publication of notice regarding submittal of this petition is included in
Appendix B.
005-01rptdoc
Page 5

 
3.0
WASTE AND WASTE MANAGEMENT HISTORY INFORMATION
3.1
DESCRIPTION OF PETITIONED WASTE
This plan covers a waste stream described as
MTR Landfill Leachate.
The F039 listing is for
a multisource leachate. The leachate is a dark colored liquid and is collected from the
primary and secondary leachate collection systems underlying the MTR hazardous waste
landfill.
Figure 3-1
provides a basic schematic of waste input and operation of the MTR Landfill.
The landfill occupies an area of approximately 17 acres and is being constructed in three
stages, one cell at a time. Cell 3 was constructed in 1990 and closed in 1995. Cell 2 was
constructed in 1995 and is currently active and receiving primarily nonhazardous solid
wastes. Currently, there are no plans to construct Cell 1. The entire landfill is scheduled for
closure by 2007.
As shown, the landfill has both a primary and secondary liner with a leachate collection
system for both. The leachate is pumped from the collection systems to two hazardous waste
storage tanks for the storage (<90-day) of primary leachate (tank T-323) and secondary
leachate (tank T-324). The leachate has been combined in tanker trucks and disposed of as
F039 listed waste at an offsite, permitted TSD facility.
The Texas Commission on Environmental Quality (TCEQ) has recently granted Shell
permission to discharge the leachate into the Houston Ship Channel via NPDES permitted
outfall R-007. The TCEQ granted this permission based on Shell's intention to have the
leachate delisted, and it will be rescinded once the delisting process is complete.
3.2
HISTORY OF WASTE GENERATION
The MTR landfill began generating leachate around 1995 (Cell 3); however, the volume has
increased substantially over the past 3-5 years. The leachate is transported offsite for disposal
at an offsite permitted TSD facility on a monthly basis. The volume of leachate
005-01rpt.doc
?
Page 6

 
NOR #065(a)
North Effluent
Treater
(NET)
NOR #017
South Effluent
Treater
(SET)
Cetl 2'
.,(aCtive)
\
Cell 1
(not constructed)
Leachate From
2° Uner
Tank Truck
to Offsite
Disposal
flIKD
Sample
Port
T-323
Leachate From
1° Uner
WASTE CURRENTLY MANAGED
(NONHAZARDOUS)
Media contaminated with process chemicals
Oil contaminated media
Coke fines
Class 1 organic solids
Storage tank bottoms
Spent filter media
Spent catalysts
Resin solid
BPA solids
WASTE PREVIOUSLY
MANAGED
CPI sludge
(D007,D008,D009,D018)
Incinerator Ash (D007,F002,F003,F005,K048)
Spent catalyst (D001,D003,D004,13018)
Sandblast grit
DEA Polymer
2° Leachate Collection
1° Leachate Collection
2° Leachate Collection
F039
Landfill
Leachate*
Nonhazardous
Primary Solids and Biosolids (b)
MTR LANDFILL
(Site 104)
NOR #159(a)
1° Leachate Collection
T-324
Note:
*Landfill Leachate is Waste Stream Targeted for Delisting
(a)
Notice of Registration - TCEQ
(b)
Predominant Waste Stream Managed in MTR Landfill
Figure 3-1
Simplified Process Flow Diagram - Landfill Leachate
Shell Oil Company'
Deer Park, Texas
DATE
?
FILE NAME
October 2002
?
Figurel-Ldwg
WORK ORDER NO:
005-01

 
generated from 1999 to 2001 is shown below:
Year
tons/year (a)
1999
3,836
2000
9,237
2001
9,306
Annual Avg.
7,460
Annual Max.
9,306
Annual Max. assuming a
14,000
50% increase
(a) Based on Annual Waste Summary Reports submitted to the Texas Natural Resource Conservation
Commission (TCEQ)
The annual maximum amount generated (as of 2001) is 9,206 tons. Shell would like to delist
a volume 50% higher than this value to allow for future additional waste generation. The
requested amount to delist in this petition is 14,000 tons (annual maximum). This is
equivalent to 16,619 cy/year using the density of water (62.4 pounds/cf) to convert.
3.3 WASTE MANAGEMENT HISTORY
The landfill leachate is removed by vacuum truck from Tanks 323 and 324 on a monthly
basis. The following hazardous waste disposal facilities have been used for offsite disposal
of the leachate since 1998:
Texas Molecular (formerly Disposal Systems Inc.)
TXD000719518
2525 Battleground Road
Deer Park, Texas 77536
Deepwell injection
Laidlaw Environmental
TXD055141378
2027 Battleground Rd
Deer Park, TX 77536
Hazardous waste incineration
Chemical Waste Management
TXD000838896
Hwy 73, 3 miles west of Taylor Bayou
P.O. Box 2563
Port Arthur, TX 77643
Incineration and Deepwell injection
005-0 I rpt.doc
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Page 8

 
Duratherm, Inc.
TXD981053770
2700 Ave. S.
San Leon, Texas 77539
Hazardous waste fuel blending and recycling
If the leachate is delisted, Shell will make piping modifications to allow the leachate to be
routed to the North Effluent Treater for treatment. The treated effluent is discharged through
an NPDES permitted outfall (Permit: TX0004871, Texas permit #00403).
005-0 1 rptdoc
Page 9

 
4.0
PROCESS AND WASTE MANAGEMENT HISTORY INFORMATION
4.1
GENERAL OPERATIONS AT THE GENERATING FACILITY
Table 4-1
provides a list of the raw products and refined products used and produced at this
refinery. Shell Oil Company refines high sulfur crude oil from Mexico to products including
gasoline, kerosene, jet fuel, fuel oil, lube oil and others. The facility occupies approximately
1600 acres in an industrial area on the south bank of the Houston Ship Channel. The Shell
refinery portion of the facility is located generally north of the railroad tracks that cross the
facility in an east/west direction.
The refinery consists of distillation, coking, cracking, reforming, hydrotreating and other
production units. The production units and their design and production capacity are shown in
Table 4-2.
4.2
OVERVIEW OF CONTRIBUTING MANUFACTURING PROCESSES
There were very few hazardous wastes managed in the MTR landfill. The hazardous wastes
included incinerator ash, spent catalysts and filters, CPI sludge from the refinery wastewater
treatment plant (North Effluent Treater) and primary solids from Shell Chemical and the
South Effluent Treater (SET). The wastes disposed of in the MTR landfill for the past four
years have been Class 1 and Class 2 nonhazardous wastes
(Table 4-3).
The following
sections describe the contributing processes that generate the predominant hazardous and
nonhazardous waste streams managed in the MTR landfill.
4.2.1 Incinerator Operations (Generates Incinerator Ash)
Shell once operated an incinerator to destroy biosolids sludge from both the refinery and
chemical wastewater treatment plants. The waste ash carried the listing D007, F002, F003,
F005, K048. Although there are no laboratory analyses available for the ash,
Table 4-4
shows the constituents that formed the basis for listing the EPA codes. It is unlikely that the
ash contained organic constituents, due to their destruction in the incinerator.
005-0 1 rpt.doc
Page 10

 
TABLE 4-1
Raw Materials, Intermediates, and Products
Shell Oil Company
Deer Park, Texas
Parameter
CAS Number
Raw Materials
Crude Oil.
8002-05-9
Major Intermediates
Intermediates are consistent with refinery operations.
Products
MTBE
1634-04-4
Unleaded Gasoline
Mixture
Butane/Butylene
106-97-8
68477-42-9
Domestic Jet Fuel
8008-20-6
Kerosene, Stove, Etc.
8008-20-6
Waxes
64742-61-6
63231-60-7
Distillate Fuel Oil
68334-30-5
Residual Fuel Oil
68476-33-5
Motor and other Lube Oils
64742-54-7
64742-18-3
Process Oils (Lubes)
64742-53-6
64742-52-5
Isobutane and other Light Process Stocks
75-28-5
Natural Gasoline
8006-61-9
Sulfur
7704-34-9
Asphaltic Products
Mixture
Propane
74-98-61
Coke
64741-79-3
005-01rptdoc
Page 11

 
TABLE 4-2
Production Units and Capacities
Shell Oil Company
Deer Park, Texas
Production Unit
Production Capacity
(in MB/SD)
(a)
Design Capacity
(in MB/SD)
Lube Crude Distillation
70.0
70.0
General Crude Distillation
204.5
210.0
Vacuum Distillation
104.5
115.0
25.0
14.0
9.5
25.0•
Delayed Coking
65.0
65.0
Catalytic cracking
67.0
70.0
Reforming:
Semi-Regen
24.5
27.0
Cyclic
47.0
47.3
Hydrocracking
67.0
68.5
Hydrotreating:
Naphtha
65.0
65.0
Kerosene
37.0
37.0
Distillate
35.0
35.0
Cat Feed
45.0
49.5
Other
41.0
44.0
Lube
12.0
13.5
Alkylation
(H2SO4)
16.8
17.2
Methyl tert-butyl ether
5.7
5.7
Asphalt
4.7
4.7
Hydrogen:
Steam/Methane Reformer
65.0
70.0
Pressure Swing Absorber
38.0
38.0
Coke (metric tons/day, 8% water)
4,122
4,122
Lube Processes:
Deasphalting
4.2
4.2
Solvent Extraction
13.0
13.0
MEK Dewaxing
7.5
10.0
Deoiling (WAX)
2.4
2.4
NOTE:(a)
MB/SD (thousand barrels per stream day) is capacity of unit on
sustained basis
005-0 I rpt.doc?
Page 12

 
TABLE 4-3
Volume of Waste Disposed of in MTR Landfill (a)
Shell Oil Company
Deer Park, Texas
Waste Type
TCEQ Waste
Code
1998
Tons
1999
Tons
2000
Tons
2001
Tons
DEA Polymer
00034031
25
0
0
0
Nonhazardous Resin Solid
01034031
655
1025
1066
0
BPA Solids
02014031
30
21.5
34
0
Chemical Primary Solids
03085031
9694
38
0
0
Biosolids – Refinery and
03056072
4479
0
0
0
Chemical Class 2
Biological Treatment
03146071
0
1544
0
0
Sludge (organic)
Sandblast Grit
07013891
232
86
0
0
Chemical Contaminated
60033011
1249
741
478
0
Media
Oil Contaminated Media
70023011
2032
1769
1351
370
Nonhazardous Catalyst
80053931
3256
573
310
1
Nonhazardous Tank
80103191
97
78
0
0
Bottoms
Nonhazardous Filter
80123101
170
105
66
0
Media
Coke Fines
80264891
101
354
0
0
Class 1 Organic Solids
80294091
218
570
27
50
Plant Trash
80203191
0
0
50
0
TOTAL
22, 238
6,904
3,382
421
NOTES:
(a) Based on Annual Waste Summary Reports
005-0 I rptdoc
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Page 13

 
TABLE 4-4
Potential Constituents in Incinerator Ash
Shell Oil Company
Deer Park, Texas
Basis for Listing (a)
D007
Chromium
F002
Tetrachloroethylene
Methylene chloride
Trichloroethylene
1,1,1-Trichloroethane
1,1,2-Trichloroethane
Chlorobenzene
Ortho-dichlorobenzene
Trichlorofluoromethane
F003
• N.A.
F005
• Toluene
Methyl ethyl ketone
Carbon disulfide
Isobutanol
Pyridine
2-ethyoxyethanol
Benzene
2-nitropropane
K048
Hexavalent chromium
• Lead
NOTE: (a)
40CFR261, Appendix VII
005-01rpt.doc
Page 14

 
4.2.2 Maintenance Activities (for spent catalysts, filters)
Many of the refinery processes use catalysts to facilitate the process and simplify the
hardware. Depending upon the process unit, spent catalyst are either hazardous or
nonhazardous. Hazardous spent catalyst is generally a listed waste from refining
hydrotreating processes. Nonhazardous spent catalyst generally is from the Catalytic
Cracking Unit (CCU).
Spent catalyst from the various hydrotreater units is generated during routine maintenance
shut-downs (turn-arounds). A turn-around usually occurs every two years at the Shell Deer
Park Refinery. The hazardous spent catalyst is usually sent off site for regeneration or
disposal.
• -
Spent catalyst from the CCU is generated as part of the process itself. New catalyst is
inserted into the CCU on a daily basis with spent catalyst generated at the same rate. The
spent catalyst is accumulated in hoppers and is disposed of every two weeks. In the past the
spent catalyst has been disposed of in the MTR landfill. Currently, it is sent off site for
recycling. The spent catalyst generally contains elevated levels of nickel and vanadium.
Nonhazardous filter media is generated during the routine maintenance of the various refinery
scrubbers. These filters are used to filter particulates from the various process and scrubber
streams throughout the refinery. DEA polymer, bisphenol acetone (BPA) solids, and filter
media are all generated as part of the amine regeneration and scrubbing process. Amine
solution is circulated through various refinery scrubbers to remove hydrogen sulfide from the
process stream.
4.2.3
Refinery Wastewater Treatment Biosolids — Nonhazardous
As shown in
Table 4-3,
biological treatment sludge (biosolids) was disposed of in the landfill
in 1999. Historical data for the sludge shows that it was disposed of in the landfill in
relatively large quantities in the past. The biosolids are generated at the North Effluent
Treater (NET) (unit number 065 on the TCEQ Notice of Registration).
Figure 4-1
illustrates
the NET treatment process and points of primary solids (CPI sludge) and biosolids
generation.
The process wastewaters treated at the NET originate from refining and lubricant
manufacturing units. Waters treated include process wastewaters, ballast waters, and water
recovered from the oil recovery system. Stormwater from the Stormwater Impoundment
Basin is also treated in the NET.
005-01rptdoc
Page 15

 
Five CPI's are located within the Refinery and at the NET. These CPI's provide the primary
oil/water/solids separation step. Process waste, ballast water, and water recovered from the
oil recovery system are all treated in the CPI's. The CPI discharge combines with stormwater
from the Stormwater Impoundment Basin prior to neutralization using caustic and sulfuric
acid. The neutralized water flows through an equalization vessel. Discharge of the
equalization vessel is influent for the dissolved air flotation (DAF) unit (Intermediate
oil/water separation). The DAF effluent is further processed through the biological treatment
processes. These processes consist of a trickle filter and/or two activated sludge basins
(North Aeration Basin, South Aeration Basin). Effluent from the basins is clarified in two
gravity bed clarifiers and deep bed, monomedia, gravity flow filters prior to discharge
through outfall R-007.
The biosolids collected off the clarifiers are processed through a thickener and digester to
reduce the water and hydrocarbon content. The sludge flows through the thickener (40-foot
diameter x 10 foot) with an average retention time of 13 hours. It is then digested in an
850,000-gallon aerobic digester for approximately 24 days. The dewatered sludge is then
either disposed of in the MTR landfill, recycled in the refinery's coker unit or sent off site for
disposal, depending on the hydrocarbon content. TCLP analyses performed in the past show
that the sludge is not a characteristic hazardous waste once it has been processed through the
thickener and digester. Recent analyses on the sludge show it is a Class 2 nonhazardous
waste.
4.2.4 Resin
Resins are no longer manufactured at the Shell Deer Park Refinery, as that business was sold
to a third party. Nonhazardous resin solids were generated at the Resins plant during the
cleanup of various spills from either the resin solidification process and/or during the bagging
operations. The spilled resin was picked up along with dust, dirt and other media during
cleanup of the process area. Resin solids also includes filter sludge, bag dust, pipe clean out
and vessel clean out of solidified resin_
4.2.5 Shell Chemical Primary Solids
Chemical primary solids consist of sludge and solids that settle in the API separators in the
Shell Chemical Plant. Primary solids, consisting of mainly calcium carbonate, also collect in
the primary clarifiers of the South Effluent Treater (SET) (unit number 017 on the NOR).
Figure 4-2
illustrates the SET wastewater treatment process. These solids may have residual
oil and resin, but are nonhazardous waste. The SET treats wastewater from the chemical
units that produce oxygenated solvents, olefins, resins, vinyl chloride monomer and phenol
005-01rpt.doc
Page 17

 
Flocculator
EWT-8
Rash Miser
EINT-7
(iorth
EWT-9
EWT-10
X-330 Sump
Acidt ?
Caustic
Equal.
X-330Tank
--I.
Biological Treatment
(
Thickener?
?
EWT-15
Clarifier
Phosphoric Acid
Skimmings
Treater
1-304
7C
latate
Storage
1-303
T-305
To
Rer-overy via
Decant Pes
— — — 0
.
Alternative Flow?
Storm Flow
Figure 4-1
NET Biotreatment System
KEY:
?
■ Normal Flow?
?
4' Diverted Flow
North P?
Storm Irripoundmen
EWT-6?
Basin
?
OAF Float
X-316Tank
?
?
;?
OAF Float
--le Manhole 04
Inside
hoer
V
To
Recovery via
Decant Pas
Recovered Oil
Acid
Caustic
CPI 02
T-307
iOF 02
T-309
orth
Aeration Basin
EWT-11
South Aeration Resin
EWT-12
-4-
HAN
HHH
'lEquTank
Static Mixer
XStH
CPI 01
1OF 01
T-306
T-308
(c
East
Clarifier
Clarifier
Water
To
Diverskin Tank
EWT-13
EWT-12
biosolids
Hydro
Wont DU-1
DIJ-l&2
X-320/11213 ?
Degas
Polymer
Recovered OH To
Discharge of CPI
04 Sump
1-301/302
Recovered Oil
biosolids
Sand Filters
EWT-17/18A-1
— To
Ponth
Nort
I • R-007
Benzene Waste NESHAP Pre-Treatment
Spill
AversionSump
?
4
4
?
?
CPI-2
CPI-1
SWS-2
MH
CCLP CPI
0
EWT-3 (A-0)
Afisy-1/MTBE
Primary Treatment
aversion
Tank
-412
DO-2 CPI
EWT-1 (A-D)
MH
MH
TCLG CPI
EWT-2 (A-13)
Digester
OM/l-16
biosolids
Trickle Fitter Sump
?

 
To Class 1
Landfill
Belt Press
Biosolids, Waste Code 0320607H
Belt Press
Primary Solids, Waste Code 0320607H
DATE
FILE NAME:
WORK ORDER NO.:
November 2002
Figurel .dwg
005-01
Chemical Sewer
1. Hazardous WW from refinery and
chemicals process, 80051021,
2.
Arninewater mixture from fuel gas
treating, 802510211.
3.
Non-hazankate WW from refinery and
chemical processes, 80041021.
4. Mon•hazercfous amlnetweler mixture
hum fuel pea treating, 80111021.
5.
Wastewater from Oxy VCM
Plant 0022105H.
6.
Wastewater from Resolution
Perfromances Products LLC
Epichlorohydrin Unit.
NPDES Outfall
(Ship Channel)
TNRCC Permit
#00402
Thickener
FIGURE 4-2
Simplified Process Flow Diagram
South Effluent Treater (SET)
Shell Chemical-Deer Park, Texas
Sludge
Recycle to Basins
Phenol Acetone Plant (PAP)
Wastewater
Secondary
Clarifier
West Basin
NOR 040
Sludge
Primary
Clarifier
Secondary
Clarifier
Middle Basin
"A"
-
? NOR 039
Splitter
Box
Direct
Chlorination
of Purge Streams
Sludge
Splitter
Box
Secondary
Clarifier
Prinary
East Basin
NOR 038

 
acetone. Chemical analysis of the primary solids (6/23/00) show that the waste is not a
characteristic hazardous waste. Because the SET treats a listed wastewater from OxyVinyls
(K017, K019, K020), the solids generated from treatment of the chemical wastewater might
be considered hazardous due to the derived-from rule. Shell is working with the TCEQ to
gain clarification on the regulatory status of these solids. OxyVinyls submitted a delisting
petition to EPA on October 11, 2002 to delist the wastewater for these waste codes.
4.2.6 Shell Chemical Biosolids
The biosolids are generated in the east, middle, and west aeration basins of the SET. They
consist of biomass and floc that form the aerobic digestion of the chemical wastewater. The
solids are separated in the three clarifiers that follow the aeration basins. Excess biosolids are
processed through a thickener and filter press and transported off site for disposal. In the
past, biosolids were disposed of in the MTR. Chemical analysis of this waste stream in June
2000 showed that the waste is not hazardous due to characteristic and the Total Petroleum
Hydrocarbon content was less than 50 mg/kg. The biosolids, like the primary solids, may
carry the K017, K019 and K020 listing until either OxyVinyls' wastewater is delisted or
regulatory status is determined.
4.2.7 Oil Contaminated Media
Oil contaminated media includes Class 1 waste consisting of soil from spill cleanups and
from construction areas contaminated with oil'(TPH). This waste also includes rags, personal
protective equipment/clothing and spent absorbents/pads/booms contaminated with
nonhazardous oil.
4.3
LANDFILL OPERATION AND LEACHATE COLLECTION SYSTEM
The MTR landfill consists of three cells, a leachate collection system and two less-than-90
days leachate storage tanks. Cell 3 was constructed in November 1990 and capped in 1995.
Cell 2 was constructed in September 1995 and is open, and Cell 1 has not been constructed.
The landfill is currently scheduled for closure in 2007.
Figure 4-3
shows a plan view of the
landfill and the leachate collection and storage system.
4.3.1 Landfill Design
The landfill is designed to meet the minimum technological requirements (MTR) specified in
40CFR264.301. This includes design requirements of a primary leachate collection system
and liner (underlying the deposited waste) followed by a secondary leachate
005-01rptdoc
Page 19

 
91.(41.•
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Figure 4-3
Plan View of Landfill and
Leachate Collection Tanks
0293.225.625
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collection system and liner (underlying the primary liner).
Figure 4-4
shows the components
of the primary and secondary leachate/liner systems.
4.3.2 Leachate Collection System Design
This landfill design includes a series of liners and leachate collection systems that envelope
the deposited waste to prevent migration of wastes and leachate out of the landfill. Just
beneath and in direct contact with the waste is the upper or primary leachate collection
system. This system includes (beginning at the top) a three-inch sand layer, a layer of
geotextile fabric, and a gravel layer whose thickness varies from 0.5 to 1.5 feet. Two eight-
inch perforated leachate collection pipes are located within the gravel layer and are in turn
contained in two east-west trenches of each half cell.
The eight-inch pipes connect on one end of the cell to a 12-inch perforated pipe which is
perpendicular to the collection pipes and is contained in a two-foot deep sump at the outer
end of each half cell. Each end of the 12-inch headers is capped. Two 12-inch stand pipes,
also referred to as well casings, connect to the sump pipe in each half cell. The stand pipes
are at right angles to the sump pipe and extend along the 1V:2H slope, following the inner
face of the perimeter dike to the top of the landfill. Leachate filters through the sand layer
into the gravel layer. The high permeability gravel layer permits the rapid flow of leachate
along a two percent slope in a north or south direction, toward the two east-west oriented
trenches. The primary leachate collection system components slope from the center dike into
a lengthwise direction in each half-cell toward the collection sumps.
The primary liner is immediately below the gravel layer. The primary liner is a single,
flexible membrane of 100-mil high-density polyethylene (11PDE) material. This liner follows
the same contours and slopes as the primary leachate collection system sand and gravel
layers. The primary liner covers the sides and the bottom of the landfill. The purpose of this
liner is to contain all leachate so that it can be collected and removed from the landfill.
If leachate penetrates the primary liner, it is collected in the secondary leachate collection
system. This system is located immediately below the primary liner and consists of a 250-mil
HDPE drainage netting (see
Figure 4-5).
The length of the leak detection system is
interrupted at intervals by 6 percent bentonite clay dams to divide the bottom area of the half
cell into compartments. In the trenches, each dam is penetrated by one to four leachate
collection/test pipes. Each of the four pipes in a trench has a different length and is
perforated only at the end position that is between dams. This means that each pipe would
005-01rpt.dac
Page 21

 
TWO LEACHATE COLLECTION SYSTEMS
SEPARATED BY LINER
2-12' HDPE STAND PIPES
GEOTEXTILE
.
?
FABRIC
12° HDPE PERFORATED
'SUMP' PIPE
3' COARSE SAND
100-MIL HDPE LINER
1'-6' GRAVEL LAYER
DRAINAGE MAT
80-MIL LINER
HDPE PERFORATED
3' LAYER OF CLAY
LEACHATE COLLECTION PIPES
.
?.
3' COARSE SAND
Figure 4-4
Primary and Secondary Leachate Collection Systems
Site 104, MTR Landfill
Isometric View

 
F: e
4-5
Secondary Leachate Collection Systems
Site 104, MTR Landfill
Isometric View
4-2" HDPE PERFORATED
LEACHATE COLLECTION
TEST PIPES
TWO LEACHATE COLLECTION SYSTEMS
SEPARATED BY LINER
4 SECTIONS OF 250-MIL
HDPE DRAINAGE
MATTING
1
100-MIL
HDPE LINER
80-MIL HDPE LINER
BENTONITE (6%) CLAY DAM
3'-0" LAYER CLAY

 
collect leachate from a single but different compartment. Utilizing this design enables the
identification of the area of the primary liner where a leak is indicated. The HDPE drainage
mat is designed to allow the rapid flow of leachate to the collection pipes below.
Beneath the drainage mat and collection pipes of the secondary leachate collection is the
secondary liner, which is an 80-mil HDPE flexible membrane and a 3-foot thick clay liner.
The HDPE liner, like the primary liner, completely covers the bottom of the cell and extends
up the side walls of the containment dikes. The flexible membrane liner is in direct contact
with and is supported by a three-foot basal clay, low permeability liner (1 x 10
-7
cm/sec
permeability). This compacted clay soil liner is designed to follow a two percent slope
toward the two east-west oriented trenches.
4.3.3 Leachate Collection Storage Tanks/Truck Loading
The storage facility consists of two 1,000-barrel aboveground storage tanks; one for leachate
collected from the primary collection system (T-323) and one for the secondary collection
system (T-324). The tanks are supported by steel structures placed on a concrete slab. The
slab is surrounded by a 3-ft high concrete retaining wall providing secondary containment. A
tank truck-loading pad is constructed outside the secondary containment area. The storage
facility is equipped with piping, valves, and pumps to load leachate into tank trucks for
offsite disposal. The storage tanks are equipped with automated level sensors to detect spills
and overfills. The two tanks have valves that allow the trucks to load either from the primary
or secondary leachate tanks, or from both simultaneously. A sample port is located between
the pump and the loading pipeline to the truck.
4.4 DESCRIPTION OF WASTE MANAGEMENT UNITS
There are 7 hazardous waste treatment and storage units at the refinery. The hazardous waste
management units include one hazardous waste landfill (MTR Landfill), three container or
dumpster storage areas, one wastewater treatment unit (NET), one waste pile, and one pond
(North Pond). The locations of these units (as identified by the NOR number) are shown in
Figure 4-6.
Some of the units are exempt from permitting. The landfill is authorized under
the RCRA Permit No. HW-50099-001, issued by the TCEQ and EPA.
Table 4-5
lists the
unit, its NOR number and the hazardous waste streams managed in each.
Hazardous wastes generated at the Shell refinery include CPI sludge, DAF solids, primary
solids and IGF float from the refinery wastewater treatment plant (i.e., North Effluent
005-01rpt.doc
Page 24

 
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Location of Waste Management Units
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TABLE 4-5
Hazardous Waste Management Units in the Refinery
Shell Oil Company
Deer Park, Texas
Hazardous Waste Management
Hazardous
TCEQ
Unit
Waste Managed Waste Code
NET Refinery WWTP
NOR
Facility 065 (a)
Waste Pile
NOR Facility 155
Groundwater, hazardous
0312102H
Spent acid solutions
8007104H
Spent caustic solutions
8008109H
Hazardous wastewater from 8019102H
refinery and chemical processes
Amine/water mixture from fuelgas 8025102H
treating units
Previously Managed at NET:
Refinery biosolids, hazardous
0302607H
Washwater with residue from
1705114H
combustion of phenol heavy ends
Wastewater contaminated with 7007102H
refinery listed waste
All nonhazardous waste
N/A
Previously Managed at Waste Pile:
Amine/water mixture from fuelgas 8025102H
treating units.
Container Storage Area-Paint Yard
Paint liquid
0704209H
NOR Facility 158
Paint solid
0705409H
MTR Landfill – Site 104
?
Nonhazardous waste
N/A
NOR Facility 159
Previously Managed at MTR:
CPI Sludge from refinery effluent 0307503H
treater
Incinerator Ash, hazardous
0311303H
Catalyst, hazardous, spent
8006393H
Spent filter media, hazardous 8013310H
Primary and biosolids from
0320607H
chemical wastewater treatment
005-01rptdoc
Page 26

 
Table 4-5
(Continued)
Hazardous Waste Management
?
Hazardous?
TCEQ
Unit
?
Waste Managed?
Waste Code
Container Storage Areas
NOR Facilities 165, 167
Paint liquid
0704209H
Paint solid
0705409H
Lab packs
0902003H
Spent acid
0903103H
Laboratory wastewater
0904105H
Contaminated soil
1701301H
Phenol heavy ends
170220811
Phenolic liquid wastes
1704208H
Spent sulfuric acid
5202602H
Heat exchanger cleaning liquids 7003114H
Clarified slurry oil storage tank 7006319H
sediment
Catalyst, spent
8006393H
Spent filter
8013310H
PCB contaminated media
8016319H
Filter media
8024404H
Pyrophoric solids
803240511
Tank seals
8038409H
Misc. listed organics
8017207H
Heat exchanger solids
7001319H
Refinery hydrotreater catalyst
7004393H
Refinery crude oil storage tank 700531911
solids
Storage tank bottoms solids, 8018319H
hazardous, from refinery and
chemical plant storage tanks
Media contaminated with lead 8039319H
IRU Polymer waste reactivated 0005403H
Broken fluorescent lightbulbs, 0906388H
containing mercury
Washwater with residue from
1705114H
combustion of phenol heavy ends
Debris contaminated with K022 1706319H
wastes
Chrome contaminated media
8009319H
005-01rpt.doe
Page 27

 
Table 4-5
(Continued)
Hazardous Waste Management
Unit
Hazardous
TCEQ
Waste Managed
Waste Code
Previously Managed at CSA:
Resin Waste
0102219H
Resin Waste
0104403H
Corrosive Solids
8031319H
Incinerator Ash, Hazardous
0311303H
ECH, liquid
0607207H
Spent Ni-Cd Batteries
0710309H
Spent acetonitrile
0001203H
North Pond
NOR Facility 102
CPI sludge from refinery BWN 0310503H
(benzene waste NESHAPS)
pretreatment unit
Leachate Storage Tanks
T-323,
Landfill leachate
0301116H
T-324
Less than 90-day tanks
NOR Facilities 185, 186
Notes:
(a) NOR = TCEQ Notice of Registration, dated 11/5/02
005-01rptdoc
Page 28

 
Treater, NET); incinerator ash; spent catalyst; spent filter media; waste paint; lab packs; spent
acids and spent caustic solutions.
A list of the hazardous wastes generated at Shell is shown in
Table 4-6
along with the TCEQ
and EPA waste codes for each. Wastes that are landfilled onsite currently or in the past are
identified with an asterisk.
A list of permits held by Shell Oil follow:
Hazardous Waste:
RCRA permit number HW50099-001
NPDES Permit:
TX0004871
TPDES Permit:
00403
Air Permit:
TX815, H60656F, H60659W
4.5
PROCESS MATERIALS AND WASTE VOLUMES
The primary raw product used in the refining process is a sour crude oil. Nickel and
vanadium-based catalysts are also used in the refining process.
The volume of the waste streams sent to the MTR landfill from 1998 through 2001 was
shown previously in
Table 4-3.
Oil contaminated media and chemical contaminated media
make up a large volume of waste disposed of in the landfill over the past four years. Spent
nonhazardous resin and catalyst also make up a large proportion of waste consistently
disposed of in the landfill. Biosolids and chemical primary solids were sporadically
disposed of in large quantities.
The volume of leachate collected from the primary and secondary containment systems is
shown in
Table 4-7
for the past three years. The volume is measured in terms of the
combined volumes from Tanks T-323 and T-324. These data were taken from monthly
manifest logs and Shell's Annual Waste Summaries submitted to the TCEQ.
As shown the amount of leachate generated and disposed of offsite has increased over the
past three years. Shell is currently investigating the source of leakage into the primary and
secondary systems. To date the maximum monthly volume generated is approximately 1,277
tons and the annual maximum is 9,306 tons. To allow for an approximate 50% increase in
volume, Shell is requesting to delist an annual maximum volume of 14,000 tons.
005-0 I rpt.doc
?
Page 29

 
TABLE 4-6
Hazardous Wastes Generated at Shell Oil Company (a)
Deer Park, Texas
Description
TCEQ
Waste
Code (b)
EPA
Waste Code
Spent acentonitrile
1RU Polymer waste reactivated
000120311
000540311
D001, D018,
D001
U003
Landfill leachate from onsite
hazardous waste landfill
0301116H
F039
DAF unit float, skim and bottoms
from refinery wastewater treater
0303205H
D018, K048
API skimmings from chemical
process units' wastewater treater
0304207H
D001, D018,
D035
CPI sludge from refinery
wastewater treater*
0307503H
D007, D008,
F037
D009, D018,
IGF float generated from refinery
wastewater induced gas floatation
units
0309205H
D018, F038
CPI sludge from Refinery BWN
pretreatment unit
0310503H
D018, F037
Groundwater, hazardous
Biosolids, chemical, hazardous
0312102H
0316607H
D018, D028,
K174
D043
API sludge, chemical, hazardous
0317609H
D018
Paint liquids waste materials
0704209H
D001, D005,
F003, F005
D035,
F002
Paint solids waste materials
0705409H
D001, D005,
F003, F005
D035,
F002
005-01rpt.doc
Page 30

 
TABLE 4-6
(continued)
TCEQ
Waste Code (b)
EPA
Waste Code
0902003H
D001,
D018,
D035,
F005
D002,
D019,
D040,
D003,
D022,
F002,
D011,
D028,
F003,
0903103H
0905316H
D001,
D009
D002, D009, D011
0906388H
D009
1701301 H
1702208H
1704208H
U002, UO31, U041,
U140, U161, U165,
D001, K022
U188
U055,
U188
1705114H
1706319H
D002,
K022
K022
5202602H
D018
7001319H
7003114H
D007,
K050
D008, K050
Description
Lab packs, hazardous, mixed
Spent acid containing mercury salts
generated during lab testing
Mercury salts and contaminated
media
Broken fluorescent bulbs containing
mercury
Soil contaminated with listed
commercial chemical product
Phenol heavy ends (distillation
bottoms) generated from the
production of phenol and acetone
from cumene
Phenolic liquid waste from loading,
drips and spills
Washwater with residue from
combustion of phenol heavy ends
Debris contaminated with K022
waste
Spent sulfolane sludge with benzene
Heat exchanger cleaning solids from
refinery exchanger cleaning
Heat exchanger cleaning liquids
from refinery exchanger cleaning
0435-01rpt.doc
Page 31

 
Catalyst, hazardous, spent*
Spent acid solution
Spent caustic solutions
Chrome contaminated media
Spent filter media contaminated
with hazardous compounds*
PCB contaminated media
8006393H
800710411
8008109H
8009319H
8013310H
801631911
Misc. listed organics from spills, 8017207H
drips, etc.
Storage tank bottom solids from 8018319H
refmery/chemical plant storage
Wastewater from refmery/chemical 8019102H
production facilities
Wastewater received from co
8022102H
located facility
Filter media contaminated with 8024404H
benzene
Amine/water mixture from fuel gas 8025102H
treating units, contains benzene
Pyrophoric solids
8032405H
TABLE 4-6
(continued)
Description
?
TCEQ
?
EPA
Waste Code (a)
?
Waste Code
Refinery hydrotreater catalyst, spent 700439311
D001, D003, D004, D018,
K171
Refinery crude oil storage sediment 7005319H
K169
Clarified slurry oil storage tank
7006319H
K170
sediment
D1,
D003, D004, D018
D002
D2,
D018
D007
D001, U002, U003, UO31,
U041, U140, U159, U161
D001
D001, D018, D035, U002,
UO31, U140, U159, U161
D001, D018, D035, K169,
K170, UO31, U140
D007, D018, D022, D026,
D028, D035, D038
K017, K019, K020
D001, D018
D018
D001
005-01rpt.doc
?
Page 32

 
TABLE 4-6
(continued)
Description
TCEQ
EPA
Waste Code (a)
Waste Code
Tank seals
8038409H
D001, D018
Media contaminated with lead
No longer generated wastes (only
listed below if it was disposed of in
the MTR Landfill)
8039319H
D008
Hazardous incinerator ash* 0311303H
D007, F002, F003, F005,
K048
Paint wastes, liquid*
910650
F002, F003, F005
Sulfur-polymer*
948880
none
Biosolids, hazardous from 0302607H
K048
refinery wastewater treater
NOTES:
(a)
Also includes wastes generated by Shell Chemical Company located within the same
complex.
(b)
TCEQ = Texas Commission on Environmental Quality
Wastes disposed of in the MTR landfill (presently or in the past).
005-0 I rpt.doc
Page 33

 
TABLE 4-7
Volume of MTR Landfill Leachate
Shell Oil Company
Deer Park, Texas
Waste Name
1999
2000
2001
Tons
Tons
Tons
MTR Landfill Leachate
3,836
9,237 9,306
MTR Landfill Leachate (a)
Monthly Avg. =
622 tons
Monthly Max. =
1,277
tons
Annual Avg. 7,460
tons
Annual Max. 9,306
tons
Shell wants to increase the maximum volume of 9,306 tons by approximately 50% to allow
for potential future leachate volumes.
9306 tons/year x 1.5
=
app. 14,000 tons/year
005-01rptdoc
Page 34

 
5.0 ANALYTICAL PLAN DEVELOPMENT
5.1 CONSTITUENTS FORMING BASIS OF LISTING
Table 5-1
shows the list of constituents for the F039 multisource leachate for which the
waste was listed in 40 CFR 261, Appendix VII. The constituents are volatile organics,
semivolatile organics, metals, pesticides, herbicides, dioxins and furans. Appendix VII of
261 refers to 40 CFR 268.43(a) for the list and states that the F039 listing includes "all
constituents for which treatment standards are specified for multisource leachate".
5.2 SELECTION OF ANALYTE LIST
As part
of the Sampling and Analysis Plan (SAP) for the petitioned waste stream, an analyte
list was developed. The components of the list were based on process knowledge and
previous analytical data. The list was reviewed and approved (with modifications) by EPA.
The analytes included on a total basis are the Appendix IX list of metals, volatiles,
semivolatiles, pesticides, herbicides, PCBs and dioxins/furans. The Appendix IX
constituents are a refined list taken from the Appendix VIII list of hazardous constituents.
The Appendix IX list includes the constituents for which the Shell waste was listed, the
constituents detected in the wastes, and any other compounds that may exist as byproducts of
combustion (i.e., for the incinerator ash disposed of in the past).
Dioxins and furans may form as a byproduct from the incineration of chlorinated aromatic
compounds such as chlorinated phenols, pesticides and PCBs (API, 1990, Dioxins and
Furans – A Primer. Pub #4506). These compounds are included in the analytical program. A
2,3,7,8-TCDD equivalent was calculated foreach set of dioxin/furan analyses using EPA
methodology.
The Appendix IX pesticides, herbicides and PCBs were included in the analyte list as a
conservative measure. These compounds are not used as raw products for contributing
processes and are not generated as a result of process operations. In accordance with Section
6.6.2 of the "EPA RCRA Delisting Program Guidance Manual for the Petitioner" the waste
streams samples were also analyzed for the following additional analyses:
Total oil and grease;
Total cyanide and sulfide;
Ignitability and corrosivity
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TABLE 5-1
Basis for Listing Hazardous Waste
40 CFR 261, Appendix VII
Shell Oil Company
Deer Park, Texas
F039
F039 (continued)
• Acenaphthene
• Carbon disulfide
Acenaphthylene
Carbon tetrachloride
Acetone
Chlordane (alpha and gamma isomers)
• Acetonitrile
p-Chloroaniline
Acetophenone
Chlorobenzene
2-Acetylaminofluorene
Chlorobenzilate
• Acrolein
2-Chloro-1,3-butadiene
• Acrylonitrile
Chlorodibromomethane
• Aldrin
Chloroethane
4-Aminobiphenyl
bis(2-Chloro-ethoxy)methane
Aniline
bis(2-chloroethyl)ether
Anthracene
Chloroform
Aramite
bis(2-Chloroisopropyl)ether
• alpha-BHC
p-Chloro-m-cresol
beta-BHC
Chloromethane (methylene chloride)
• delta-BHC
2-Chloro-naphthalene
ganuna-BHC
2-Chlorophenol
Benzene
3-Chloropropylene
Benz(a)anthracene
Chrysene
• Benzo(b)fluoranthene
o-Cresol
Benzo(k)fluoranthene
m-Cresol
Benzo(g,h,i)perylene
p-Cresol
Benzo(a)pyrene
Cyclohexanone
• Bromodichloromethane
1,2-Dibromo-3-chloropropane
Methyl bromide (bromomethane)
Ethylene dibromide
• 4-Bromophenyl phenyl ether
Dibromomethane
• n-Butyl alcohol
2,4-D
Butyl benzyl phthalate
o,p'-DDD
2-sec-Butyl-4-6-dinitrophenol (dinoseb)
p,p'-DDD
o,p'-DDE
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TABLE 5-1
Basis for Listing Hazardous Waste
40 CFR 261, Appendix VII
Shell Oil Company
Deer Park, Texas
F039
F039 (continued)
-1 - -
p,p'-DDE
o,p'-DDT
p,p'-DDT
Dibenz(a,h)anthracene
Dibenz(a,e)pyrene
m-Dichlorobenzene
o-Dichlorobenzene
p-Dichlorobenzene
Dichlorodifluoromethane
1,1-Dichloroethane
1,2-Dichloroethane
1,1-Dichloroethylene
trans-1,2-Dichloroethylene
2,4-Dichlorophenol
2,6-Dichlorophenol
1,2-Dichloropropane
cis-1,3-Dichloropropylene
trans-1,3-Dichloropropylene
Dieldrin
Diethyl phthalate
2-4-Dimethyl phenol
Dimethyl phthalate
Di-n-butyl phthalate
1,4-Dinitrobenzene
4,6-Dinitro-o-cresol
2,4-Dinitrophenol
2-4-Dintrotoluene
2,6-Dinitrotoluene
Di-n-octyl phthalate
Di-n-propylnitrosamine
1,4-Dioxane
Diphenylamine
Diphenylnitrosamine
1,2-Diphenylhydrazine
Disulfoton
Endosulfan
Endosulfan
Endosulfan sulfate
Endrin
Endrin aldehyde
Ethyl acetate
Ehtyl cyanide (propanenitrile)
Ethyl ether
bis(2-Ethylhexyl)phthalate
Ethyl methacrylate
Ethylene oxide
Famphur
Fluoranthene
Fluorene
Heptachlor
Heptachlor epoxide
Hexachlorobenzene
Hexachlorobutadiene
Hexachlorocyclopentadiene
HxCDDs (all dioxins)
HxCDF (all furans)
Hexachloroethane
Hexachloropropylene
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TABLE 5-1
Basis for Listing Hazardous Waste
40 CFR 261, Appendix VII
Shell Oil Company
Deer Park, Texas
F039
F039 (continued)
••
Indeno
Iodomethane(1,2,3-c,d)pyrene
ParathionN-Nitrosopyrrolidine
Isobutyl alcohol
Total PCBs
Isodrin
Pentachlorobenzene
Isosafrole
PeCDDs
Kepone
PeCDFs
Methacrylonitrile
Pentachloronitrobenzene
Methanol
Pentachlorophenol
Methapyrilene
Phenacetin
Methoxychlor
Phenanthrene
3-Methylcholanthrene
Phenol
4,4-Methylene bis(2-chloroaniline)
Phorate
Methyl ethyl ketone
Phthalic anhydride
Methyl isobutyl ketone
Pronamide
Methyl methacrylate
Pyrene
Methyl methansulfonate
Pyridine
Methyl parathion
Safrole
Naphthalene
Silvex (2,4,5-TP)
2-Naphthylarnine
2,4,5-T
p-Nitroaniline
1,2,4,5-Tetrachlorobenzene
Nitrobenzene
TCDDs
5-Nitro-o-toluidine
TCDFs
p-Nitrophenol
1,1,1,2-Tetrachloroethane
N-Nitrosodiethylamine
1,1,2,2-Tetrachloroethane
N-Nitrosodimethylamine
Tetrachloroethylene
N-Nitroso-di-n-butylamine
2,3,4,6-Tetrachlorophenol
N-Nitrosomethylethylamine
Toluene
N-Nitrosomorpholine
Toxaphene
N-Nitrosopiperidine
Tribromomethane (bromoform)
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TABLE 5-1
Basis for Listing Hazardous Waste
40 CFR 261, Appendix VII
Shell Oil Company
Deer Park, Texas
F039
F039 (continued)
1,2,4-Trichlorobenzene
Antimony
1,1,1-Trichloroethane
Arsenic
1,1,2-Trichloroethane
Barium
Trichloroethylene
Beryllium
Trichloromonofluoromethane
Cadmium
2,4,5-Trichlorophenol
Chromium (total)
2,4,6-Trichlorophenol
Cyanides (total)
1,2,3-Trichloropropane
Cyanides (amenable)
1,1,2-Trichloro-1,2,2-trifluoroethane
Fluoride
tris(2,3-Dibromopropyl)phosphate
Lead
Vinyl chloride
Mercury
Xylenes (sum of o,m,p isomers)
Nickel
Selenium
Silver
Sulfide
Thallium
Vanadium
Notes: For F039 wastes, the basis of listing is "all constituents for which treatment standards
are specified for multi-source leachate under 40CFR 268.43(a), Table CCW".
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39

 
Because the waste stream is a liquid, no TCLP extraction/analyses were necessary. All
analyses were performed on a total basis.
Table
5-2
shows the analytical program for characterizing the MTR Landfill Leachate in
2002. All analytical methods are from EPA SW-846 Test Methods for Evaluating Solid
Waste-Physical and Chemical Methods.
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TABLE 5-2
Target Compounds for Waste Characterization
Shell Oil Company
Deer Park, Texas
Constituents
EPA Method (a)
Appendix IX Analyses
?
Volatiles
8260B
•?
Semivolatiles (including PCBs, Pesticides, Herbicides
8270C
•?
Metals (b)
'.
.
.
1
'
6010 for all but the
following metals
•?
7470A mercury
•?
6020 arsenic
•?
6020 lead
•?
6020 selenium
•?
Herbicides (chlorinated)
8151A
?
Pesticides (chlorinated and organophosphorus))
8081A/8141A
•?
PCBs
8082
•?
Dioxins/Furans
1613B
Hazardous Waste Characteristics/Other
Ignitability
1010
pH
150.1
Reactive Sulfide
(not required per EPA Pre-Petition Delisting Meeting)
Not required
Reactive
Cyanide(not
required per EPA Pre-Petition Delisting Meeting)
Not required
Total Cyanide
9012A
Total Sulfide
376.1
Total Oil and Grease
1664
Flouride
300
Methanol
8000
NOTES:
(a)
Test Methods for Evaluating Solid Waste-Physical and Chemical Methods,
EPA SW-846. Methods for Chemical Analysis of Water and Wastes,
EPA-600/4-79-020.
(b)
Appendix IX Metals were run on samples with pH adjustments to pH2, pH7 and pH9
on one of the four samples collected. (per EPA Pre-Petition Delisting Meeting).
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6.0
WASTE SAMPLING INFORMATION
6.1
SAMPLING PERSONNEL INFORMATION
The landfill leachate was sampled by the following contractor:
Mr. Stephen Roach
On Site Hazardous Waste Coordinator
ONYX-Environmental Services
1800 S. Highway 146
Baytown, Texas 77520
6.2
SAMPLING STRATEGY
Sampling was conducted in accordance with a written sampling plan (dated April 10, 2002)
and approved by the EPA in a letter dated May 31, 2002. Sample integrity was assured by
following standard sample handling, preservation, documentation and custody procedures
(see Sections 6.4 through 6.7). A total of eight samples and one duplicate were collected for
characterization.
6.3
SAMPLE COLLECTION AND IDENTIFICATION
Four samples of the primary leachate and four samples of the secondary leachate were
collected for characterization from June 2002 through October 2002. The sampling
procedures in the Sampling and Analysis plan were modified to incorporate EPA's comments
to sample and characterize the primary and secondary leachate separately (site visit May 2,
2002). Procedures were followed and documented to show that each leachate collection tank
had a complete turnover between each sampling event.
Table C-1
in Appendix C documents
the volume of leachate removed from each tank prior to each sampling event. This procedure
ensured that four separate samples of leachate were collected from each tank rather than
multiple samples from one tank volume of leachate.
6.3.1 Initial Sample
The valve to tank T-323 (primary leachate) was opened by the operator and about 1-liter of
leachate was purged and added back to the tank. The sample was then collected directly into
the sample bottles from the sample port. The sample for volatile analyses was collected first
by slowly filling two 40-mL VOA vials with little to no turbulence. There was no headspace
in the VOA vials when filled. The remaining bottles were then filled from the sample port.
For metals analysis, the sample was collected into three bottles containing no preservative.
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Instructions were added to the chain-of-custody form for the laboratory to adjust the pH to 2,
7 and 9 upon receipt. The date and time of collection was noted on each bottle and in the
field notebook. The sample I.D. was
T323-1.
This procedure was repeated with tank T-324
(secondary leachate) except the sample I.D. was
T324-1
6.3.2 Second Sample
Prior to collecting a second sample from the leachate tanks, at least one tank volume (per
tank) was removed for disposal off site. The volume of leachate removed from each tank was
documented. These log sheets are with the laboratory analytical reports in Appendix C to this
petition. The samples were collected following the same procedures described above except
that only one bottle for metals was filled for each sample. The bottle for metals contained
preservative to adjust the sample pH to less than 2.0. I The sample I.D.s were
T323-2 and T324-2. The dates and times of sample collection were noted on the labels, field
notebook and volume log form.
6.3.3 Third Sample and Duplicate
The third sampling event was conducted following the above procedures. The sample I.D.s
were
T323-3
and
T323-4.
The date and time of collection was noted on the sample labels,
logbook and volume log form.
6.3.4 Fourth Sample
The fourth sampling event was conducted following the procedures in Section 6.3.2. A
duplicate sample was collected from tank T-324 for QA/QC analysis. The fourth sample
I.D.s were T323-4,
T324-4A
and T324-4B. The dates and times of sample collection were
noted on the labels, field notebook and volume log form.
Resample Event
Due to anomalous readings for nickel in the fourth primary sample and methanol in the fourth
secondary sample, a resample event was conducted on December 23, 2002. These samples
I.D.s were
Primary
and
Secondary.
The dates and times of sample collection were noted on
the labels, field notebook and volume log form.
6.4
SAMPLE PRESERVATION AND HANDLING
All samples were placed in clean containers provided by the laboratory. Sample
preservatives were provided in the sample containers by the analytical laboratory.
Table 6-1
shows the containers, preservation, and EPA holding times for the samples. Once the
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TABLE 6-1
Sample Containers, Preservation and Holding Times
Shell Oil Company
Deer Park, Texas
Analysis
Sample Size/Container
(Plastic/Glass)
Preservation
Holding Time
Appendix IX Volatiles
2 x 40 ml glass vials
Cool to 4°C
14 days
HC1 to pH
<
2
Appendix IX
2 x 1,000 ml glass
Cool to 4°C
7/40 (a).
Semivolatiles
Na2S2O3
Appendix IX
4x 1,000 ml glass
Cool to 4°C
7/40 (a)
Pesticides/Herbicides
PCBs
Ignitability
1 x 500 ml plastic/glass
Cool to 4°C
28 days
pH
50 ml/plastic or glass
Cool to 4°C
Analyze immediately
Oil and Grease
1 x 1,000 ml glass
H2SO4
to pH<2
28 days
Total Sulfide
1 x 500 ml glass/plastic Cool to 4°C
7 days
Zinc acetate,
NaOH to pH>9
Total Cyanide
1 x 1000 nil glass/plastic Cool to 4°C
14 days
Ascorbic acid,
NaOH to pH> 12
Appendix IX Metals
500 ml/plastic or glass
HNO3
to pH
<
2
6 months except
mercury (28 days)
for pH7 and pH9
(2) 500 ml/plastic or
No preservative
same as above
(initial sample only)
glass
(b)
Appendix IX
2 x 1,000 ml/glass
Cool to 4°C
40 days/40 days
Dioxins/Furans
NOTES:
(a)
7/40 = Extract within 7 days of collection, analyze within 40 days of extraction.
(b)
Request on chain-of-custody form that sample pH be adjusted in the lab to pH 7 and pH 9.
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samples were collected, they were secured in an ice chest with a completed chain-of-custody
form. The cooler were sealed with tape and was picked up by the laboratory.
6.5 SAMPLING DOCUMENTATION
To prevent misidentification of samples, labels were attached to each sample container. The
labels were water proof and legible contained the following information:
Sample identification number
Date and time of collection
Sample description
Name of sampler
Analysis to be performed
A bound field notebook was maintained to provide daily records of significant events,
observations, and measurements. All entries were made using a pen or indelible marker. The
field notebook documented the following:
Date
and time of sampling event
Name of sample collector
Process sampled
Description of waste
Sample location
Sampling method
Number, volume, and appearance of sample
Sample preservation
Any field measurements made
Field observations
6.6
SAMPLE CUSTODY
Chain-of-custody procedures were used to trace possession and handling of individual
samples from the time of collection in the field through receipt by the independent analytical
laboratory.
Each time a batch of samples was prepared for pickup by the laboratory, a chain-of-custody
record was completed and accompanied the shipment. Whenever custody of the samples was
transferred, the individual relinquishing and the individual receiving the samples signed,
dated, and noted the time on the form. The original form accompanied the shipment to the
laboratory and was returned to the Project Manager with the analytical laboratory reports.
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If a delivery or courier service was used to transport the samples, the bill of lading or receipt
from the independent service was maintained by the Project Manager to document custody
for that segment of the sample transport.
6.7
QUALITY ASSURANCE/QUALITY CONTROL PROCEDURES
Each of the samples analyzed was subjected to extensive quality control. Quality control
procedures in the field included sample handling and documentation protocols as described
previously. Techniques were used in the field to avoid sample contamination and to
adequately preserve each sample until it reached the laboratory. There was no sampling
equipment associated with tank sampling, as samples were collected directly into the sample
containers. Decontamination of equipment was not necessary (equipment rinsate samples
were not necessary).
Sampling personnel wore disposal nitrile gloves to reduce the possibility of cross
contamination. Sample bottles were laboratory-precleaned containers that met cleaning QC
requirements.
Trip blanks, consisting of laboratory grade deionized water were supplied by the laboratory.
These blanks were carried with the sample containers during the first week and last week of
sample collection. The Trip Blanks were analyzed for Appendix IX VOA analyses. The
purpose of the trip blanks was to determine the impact, if any, of ambient VOC
concentrations in the refinery and laboratory during sampling and analysis.
Additional quality control procedures were employed in the laboratory. As a minimum,
laboratory QA/QC procedures were in accordance with the guidelines in Volume One,
Chapter One of EPA document SW-846. Laboratory QA/QC samples included method blank
analyses, surrogate spikes and calibration curves. A discussion of the laboratory and field
QA/QC data is presented in the Quality Assurance Report in
Appendix
A to this Delisting
Petition.
6.8
STATEMENT OF REPRESENTATIVENESS OF SAMPLES
Based on the sampling strategy discussed in Section 6.2 (and in the SAP) and the use of EPA
approved methods to collect, analyze and maintain proper documentation and custody of the
samples, the samples of primary and secondary landfill leachate collected in 2002 are
considered representative of the petitioned waste stream. There were no deviations from the
SAP dated April 10, 2002 and revised May 15, 2002 during the June 2002-December 2002
sampling events (except the duplicate was collected from Round 4 instead of Round 3).
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7.0
WASTE ANALYSIS INFORMATION
7.1
ANALYTICAL LABORATORY INFORMATION
The following laboratories were used for analysis of samples collected in support for this
delisting petition:
Severn Trent Laboratories, Inc. (STL)
6310 Rothway Street
Houston, Texas 77045
Phone: (713) 690-4444
Severn Trent Laboratories, Inc. (STL)
14046 Summit Drive
Austin, Texas 78728
(512) 244-0855
*For analysis of organophosphorous pesticides
Alta Analytical
Laboratory
5070 Robert J. Mathew Parkway
El Dorado Hills, California 95762
Phone: (916) 933-1640
* For analysis of Dioxin/Furans
STL Houston performed all analyses except those indicated with an asterisk (*). The
professional qualifications for the individuals who performed the analyses of the waste
samples are included in
Appendix D.
The Quality Assurance Report in
Appendix
A
contains information relating to the laboratory
handling and analysis procedures employed for the waste samples. Included in
Appendix
A
are
the Sample I.D., laboratory I.D., sample preservation technique, sample collection dates
and dates of sample extraction and analysis. The specific equipment used is coded to an
equipment list in the Quality Assurance Report. A list of the analytical methods used for
each of the analyses is also included in the Quality Assurance Report.
7.2
SUMMARY OF ANALYTICAL RESULTS
This section summarizes the results of analyses performed on samples collected from the
petitioned waste stream from June 2002 through December 2002. A copy of the laboratory
analytical reports are included as
Appendix C.
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7.2.1 Hazardous Waste Characteristics
A summary of the results of analyses for reactivity, ignitability and corrosivity is included in
Table 7-1.
As shown, none of the samples exhibit hazardous waste characteristics as defined
by 40 CFR 261.22 and 261.23.
Table
7-2 and
Table
7-3 compare the concentrations of the
TCLP constituents in the primary and secondary leachate, respectively, to the maximum
TCLP levels found in 40 CFR 261.24. As shown, none of the constituents in the primary or
secondary leachate exceed the maximum allowable TCLP concentrations and the landfill
leachate is not hazardous due to the toxicity characteristic.
7.2.2 Appendix IX Analytes Detected on a Total Basis
Summaries of the constituents detected in the MTR Landfill Leachate, are presented in
Table 7-4
and Table 7-5 for the primary and secondary leachate, respectively. Only those
constituents detected above the limit of quantitation (LOQ) are shown for the volatile and
semivolatile organics.
Volatile Organics
The volatile organic analyses were run on grab samples collected from the Primary Leachate
Tank (T323) and from the Secondary Leachate Tank (T324). As shown very few volatiles
were detected.
Semivolatile Organics, PCBs, Pesticide, Herbicides, and Dioxin/Furans
Tables
7-4 and 7-5 present a summary of the semivolatile constituents, pesticides, herbicides,
PCBs and dioxin/furan results for the primary and secondary leachate samples. For the
dioxin/furan results, EPA Region 6 recommends calculating a toxicity equivalent quotient
(TEQ) for 2,3,7,8-tetrachlorodibenzo(p)dioxin (TCDD). The toxicity equivalent quotient is
calculated by converting the 17 dioxin/furan congener concentrations to a 2,3,7,8-TCDD
concentration using toxicity equivent factors (TEFs). The TEFs for the 17 congeners are
listed in EPA Region 6 Delisting Technical Support Document (8/31/02). The 2,3,7,8-TCDD
equivalent calculation spreadsheets are in Appendix E for the sampling events. The
calculated 2,3,7,8-TCDD values are shown in
Tables
7-4 and 7-5. These values are
compared to EPA's delisting value for this constituent.
Metals
A summary of the Appendix IX metals detected in the samples over the sampling period is
shown in Table 7-6 and
Table
7-7 for the primary and secondary leachate, respectively.
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During the first week of sampling, three samples were collected for pH adjustment to pH2,
pH 7 and pH9 prior to analysis for metals. This procedure was required by EPA to simulate
leachate from a landfill. In accordance with the approved SAP this procedure was conducted
on only one set of samples. A review of the data in
Tables 7-6
and 7-7 show that the pH
variance did not appear to affect the concentration of the metals in the samples.
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TABLE 7-1
Summary of Reactivity, Corrosivity, and Ignitability Analyses
MTR Landfill Leachate
Shell Oil Company
Deer Park, Texas
Sample ID
Concentration
Date
Collected
Total
Sulfide
(mg/L)
Total
Cyanide
(µ0-)
pH
(Std. Units)
Ignitability
(Flashpoint)
(Degrees F)
T323-1 Primary Leachate No. 1
6/11/2002
23
<10.0
7.80
>212
T324-1 Secondary Leachate No. 1
6/11/2002
<5.0
<10.0
7.64
>212
T323-2 Primary Leachate No. 2
8/1/02
50
<10.0
7.91
>212
T324-2 Secondary Leachate No. 2
9/4/02
19
<50
8.41
>212
T323-3 Primary Leachate No. 3
9/6/02
22
<10.0
NA
>212
T324-3 Secondary Leachate No. 3
10/14/02
6.8
<10.0
7.4
>212
T323-4 Primary Leachate No. 4
9/27/02
110
<10.0
7.5
>212
T324-4A Secondary Leachate No. 4
10/24/02
16
<10.0
7.53
>212
T324-4B (Dup) Secondary Leachate No. 4
10/24/02
15
<10.0
7.37
>212
Hazardous Waste Criteria
>500 mg/kg
>250 mg/kg
..

2 or _

.12.5
<140°F
(40 CFR 261.21-261.23)
Notes:
<## = Not detected above the indicated laboratory Limit of Quantitation.
(a)
Oil and Grease concentrations ranged from <5.0 mg/L to 8.2 mg/L in T323 samples and from
5.0 mg/L to 230 mg/L in T324 samples.
(b)
Fluoride concentrations were <0.30 mg/L in T323 samples and ranged from <0.30 mg/L to 0.54 mg/L in T324
samples.
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TABLE 7-2
Summary of Toxicity Characteristic Analyses
MTR Landfill Leachate - Primary (T-323)
Shell Oil Company
Deer Park, Texas
Contaminant
Regulatory
Level (mg/L)
(a)
T323-1
6/11/2002
(mg/L)
T323-2
8/1/2002
(m811-)
T323-3
9/6/2002
(mg/L)
T323-4
9/27/2002
(mg/L)
Arsenic
5.0
<0.010
0.0294
0.0148
<0.05
Barium
100.0
0.119
0.237
0.108
0.072
Benzene
0.5
<0.005
0.018
<0.05
0.008
Cadmium
1.0
<0.005
I
<0.010
<0.005
<0.005
Carbon tetrachloride
0.5
<0.005
<0.005
<0.05
<0.005
Chlordane
0.03
<0.00005
<0.00005
<0.0001
<0.00005
Chlorobenzene
100.0
<0.005
<0.005
<0.05
<0.005
Chloroform
6.0
<0.005
<0.005
<0.05
<0.005
Chromium
5.0
<0.010
0.014
<0.010
<0.010
o-Cresol
200.0
<0.010
<0.0015
<0.0015
<0.0015
rn-Cresol
200.0
<0.010
<0.0015
<0.0015
<0.0015
p-Cresol
200.0
0.020
0.028
0.00184
0.0127
Cresol
200.0
0.020
0.028
0.00184
0.0127
2,4-D
10.0
<0.005
<0.001
<0.001
<0.001
1,4-Dichlorobenzene
7.5
<0.010
<0.002
<0.002
<0.002
1,2-Dichloroethane
0.5
<0.005
<0.005
<0.05
<0.005
1,1-Dichloroethylene
0.7
<0.005
<0.005
<0.05
<0.005
2,4-Dinitrotoluene
0.13
<0.010
<0.0015
<0.0015
<0.015
Endrin
0.02
<0.0001
<0.0001
<0.0002
<0.001
Heptachlor (and its Epoxide)
0.008
<0.00005
<0.00005
<0.0001
<0.00005
Hexachlorobenzene
0.13
<0.010
<0.0015
<0.0015
<0.0015
Hexachlorobutadiene
0.5
<0.010
<0.002
<0.002
<0.002
Hexachloroetharte
3.0
<0.010
<0.002
<0.002
<0.002
Lead
5.0
<0.003
<0.010
<0.003
<0.015
Lindane
0.4
<0.00005
<0.00005
<0.0001
<0.00005
Mercury
0.2
<0.0002
<0.0002
<0.0002
<0.0002
Methoxychlor
• 10.0
<0.0005
<0.0005
<0.001
<0.0005
Methyl ethyl ketone
200.0
<0.010
<0.010
<0.100
<0.010
Nitrobenzene
2.0
<0.010
<0.0015
<0.0015
<0.0015
Pentachlorophenol
10.0
<0.050
<0.0015
<0.0015
<0.0015
Pyridine
5.0
<0.010
<0.004
<0.004
<0.004
Selenium
1.0
0.008
0.0151
0.0086
<0.025
Silver
5.0
<0.010
<0.010
<0.010
<0.010
Tetrachloroethylene
0.7
<0.005
<0.005
<0.05
<0.005
Toxaphene
0.5
<0.005
<0.005
<0.010
<0.005
Trichloroethylene
0.5
<0.005
<0.005
<0.05
<0.005
2,4,5-Trichlorophenol
400.0
<0.010
<0.002
<0.002
<0.002
2,4,6-Trichloroprophenol
2.0
<0.010
<0.002
<0.002
<0.002
2,4,5-TP (Silvex)
1.0
<0.005
<0.001
<0.001
<0.001
Vinyl Chloride
0.2
<0.010
<0.010
<0.100
<0.010
Notes:
(a)
Maximum concentration of constituents for the Toxicity Characteristic 40 CFR 261.24 Table 1.
(b)
The maximum concentration is shown in
bold and italics.
005-0 I rpt.doc
?
Page 51

 
TABLE 7-3
Summary of Toxicity Characteristic Analyses
MTR Landfill Leachate - Secondary (T-324)
Shell Oil Company
Deer Park, Texas
Contaminant
Regulatory
Level (mg/L)
(a)
T324-1
6/11/2002
(mg/L)
T324-2
9/4/2002
(mg/L)
T324-3
10/14/2002
(mg/L)
T324-4A
10/24/2002
(mg/L)
T324-4B
(Dup)
10/24/2002
(mg/L)
Arsenic
5.0
<0.010
<0.010
<0.010
<0.010
<0.010
Barium
100.0
0.10
0.114
0.199
0.313
0.326
Benzene
0.5
<0.005'
0.006
0.014
<0.005
<0.005
Cadmium
1.0
<0.005
<0.005
<0.005
<0.005
<0.005
Carbon tetrachloride
0.5
<0.005
<0.005
<0.005
<0.005
<0.005
Chlordane
0.03
<0.00005
<0.0005
<0.0005
<0.00005
<0.00005
Chlorobenzene
100.0
<0.005
<0.005
<0.005
<0.005
<0.005
Chloroform
6.0
<0.005
<0.005
<0.005
<0.005
<0.005
Chromium
5.0
<0.010
<0.010
<0.010
<0.010
<0.010
o-Cresol
200.0
<0.010
<0.0075
<0.0015
<0.0015
<0.0015
m-Cresol
200.0
<0.010
<0.0075
<0.0015
<0.0015
<0.0015
p-Cresol
200.0
<0.010
<0.0075.
<0.0015
<0.0015
0.00414
Cresol
200.0
<0.010
<0.0075
<0.0015
<0.0015
0.00414
2,4-D
10.0
<0.001
<0.001
<0.001
<0.001
<0.001
1,4-Dichlorobenzene
7.5
<0.010
<0.010
<0.002
<0.002
<0.002
1,2-Dichloroethane
0.5
<0.005
<0.005
0.014
0.017
0.018
1,1-Dichloroethylene
0.7
<0.005
<0.005
<0.005
<0.005
<0.005
2,4-Dinitrotoluene
0.13
<0.010
<0.0075
<0.0015
<0.0015
<0.0015
Endrin
0.02
<0.00001
<0.0001
<0.0001
<0.0001
<0.0001
Heptachlor (and its Epoxide)
0.008
<0.00005
<0.00005
<0.00005
<0.00005
<0.00005
Hexachlorobenzene
0.13
<0.010
<0.0075
<0.0015
<0.0015
<0.0015
Hexachlorobutadiene
0.5
<0.010
<0.010
<0.002
<0.002
<0.002
Hexaehloroethane
3.0
<0.010
<0.010
<0.002
<0.002
<0.002
Lead
5.0
<0.003
<0.003
0.0083
<0.003
<0.003
Lindane
0.4
<0.00005
<0.00005
<0.00005
<0.00005
<0.00005
Mercury
0.2
<0.0002
<0.0002
<0.0002
<0.0002
<0.0002
Methoxychlor
10.0
<0.0005
<0.0005
<0.0005
<0.0005
<0.0005
Methyl ethyl ketone
200.0
<0.010
<0.010
<0.010
<0.010
<0.010
Nitrobenzene
2.0
<0.010
<0.0075
<0.0015
<0.0015
<0.0015
Pentachlorophenol
100.0
<0.050
<0.0075
<0.0015
<0.0015
<0.0015
Pyridine
5.0
<0.010
<0.020
<0.004
<0.004
<0.004
Selenium
1.0
0.0078
<0.005
0.0053
<0.005
<0.005
Silver
5.0
<0.010
<0.010
<0.010
<0.010
<0.010
Tetrachloroethylene
0.7
<0.005
<0.005
<0.005
<0.005
<0.005
Toxaphene
0.5
<0.005
<0.005
<0.005
<0.005
<0.005
Trichloroethylene
0.5
<0.005
<0.005
<0.005
<0.005
<0.005
2,4,5-Trichlomphenol
400.0
<0.010
<0.010
<0.002
<0.002
<0.002
2,4,6-Trichloroprophenol
2.0
<0.010
<0.010
<0.002
<0.002
<0.002
2,4,5-TP (Silvex)
1.0
<0.001
<0.001
<0.001
<0.001
<0.001
Vinyl Chloride
0.2
<0.010
<0.010
<0.010
<0.010
<0.010
Notes:
(a)
Maximum concentration of constituents for the Toxicity Characteristic 40 CFR 261.24 Table 1.
(b)
The maximum concentration is shown in
bold and italics.
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TABLE 7-4
Summary of Appendix IX Organic Constituents Detected
MTR Landfill Leachate - Primary (T-323)
Shell Oil Company
Deer Park, Texas
Sample ID:
T323-1
T323-2
T323-3
T323-4
Units:
(mg/L)
(mg/L)
(mg/L)
(ng/L)
Sample Collected:
(6/11/2002)
(8/1/2002)
(9/6/2002)
(9/27/2002)
Appendix IX Volatiles
I
Acetone
0.030
0.030
<0.100
0.020
Benzene
<0.005
0.018
<0.050
0.008
Toluene
<0.005
0.600
<0.050
<0.005
Methanol
<2.5
<2.5
<2.5
<2.5
Appendix IX Semivolatiles
4-Methylphenol (p-cresol)
0.020
0.028
0.00184
0.013
Naphthalene
<0.010
0.0317
<0.002
<0.002
2,4-Dimethyl phenol
<0.010
0.0041
<0.0015
0.0019
Phenol
<0.010
0.0352
0.0081
0.015
Acetophenone
<0.010
<0.0015
0.00303
0.0016
Phenanthrene
<0.010
<0.0015
<0.0015
0.0052
Fluorene
<0.010
<0.0015
<0.0015
0.00165
Bis (2-ethylhexyl)phthalate
<0.010
<0.0015
<0.0015
0.0037
Appendix IX
Organochlorine Pesticides (all
non detects)
Aldrin
<0.00005
<0.00005
<0.0001
<0.00005
alpha-BHC
<0.00005
<0.00005
<0.0001
<0.00005
beta-BHC
<0.00005
<0.00005
<0.0001
<0.00005
gamma-BHC (Lindane)
<0.00005
<0.00005
<0.0001
<0.00005
delta-BHC
<0.00005
<0.00005
<0.8001
<0.00005
Chlordane
<0.00005
<0.00005
<0.0001
<0.00005
alpha-Chlordane
<0.00005
<0.00005
<0.0001
<0.00005
gamma-Chlordane
<0.00005
<0.00005
<0.0001
<0.00005
4,4'-DDD
<0.0001
<0.0001
N/A
<0.0001
4,4'-DDE
<0.0001
<0.0001
N/A
<0.0001
4,4'-DDT
<0.0001
<0.0001
N/A
<0.0001
Dieldrin
<0.0001
<0.0001
<0.0002
<0.0001
Endosulfan I
<0.00005
<0.00005
<0.0001
<0.00005
Endosulfan II
<0.0001
<0.0001
<0.0002
<0.0001
Endosulfan sulfate
<0.0001
<0.0001
<0.0002
<0.0001
005-01rpt.doc
Page
53

 
Table 7-4
(continued)
Sample ID:
T323-1
T323-2
T323-3
T323-4
Units:
(m8/1-)
(mg/L)
(mg/L)
(mg/L)
Sample Collected:
(6/11/2002)
(8/1/2002)
(9/6/2002)
(9/27/2002)
Endrin
<0.0001
<0.0001
<0.0002
<0.0001
Endrin aldehyde
<0.0001
<0.0001
<0.0002
<0.0001
Heptachlor
<0.00005
<0.00005
<0.0001
<0.00005
Heptachlor epoxide
<0.00005
<0.00005
<0.0001
<0.00005
Methoxychlor
<0.0005
<0.0005
<0.001
<0.0005
Toxaphene
<0.005
<0.005
<0.010
<0.005
Kepone
<0.0025
<0.0025
<0.005
<0.0025
Appendix IX Organophosphorus
Pesticides (all non detects)
Disulfoton
N/A
<0.0002
<0.0019
<0.0002
Phorate
N/A
<0.0002
<0.0019
<0.0002
Dimethoate
N/A
<0.0002
<0.0019
<0.0002
Methyl parathion
N/A
<0.0002
<0.0019
<0.0002
Ethyl parathion
N/A
<0.0002
<0.0019
<0.0002
Famphor
N/A
<0.0002
<0.0019
<0.0002
Sulfotepp
N/A
<0.0002
<0.0019
<0.0002
0,0,0-
N/A
<0.0002
<0.0019
<0.0002
Triethylphosphorothioate
Appendix IV Herbicides (all non
detects)
2,4-D
<0.005
<0.001
<0.001
<0.001
2,4,5-TP
<0.005
<0.001
<0.001
<0.001
2,4,5-T
<0.005
<0.001
<0.001
<0.001
Appendix IX PCBs (all non
detects)
Arochlor 1016
<0.001
<0.00095
<0.001
<0.001
Arochlor
1221
<0.001
<0.00095
<0.001
<0.001
Arochlor 1232
<0.001
<0.00095
<0.001
<0.001
Arochlor 1242
<0.001
<0.00095
<0.001
<0.001
Archolor 1248
<0.001
<0.00095
<0.001
<0.001
Arochlor 1254
<0.001
<0.00095
<0.001
<0.001
Arochlor 1260
<0.001
<0.00095
<0.001
<0.001
Appendix IX Dioxins/Furans
2,3,7,8-TCDD Equivalent
2.45E-09
2.13E-09
4.47E-09
3.24E-09
Notes:
<#41= Not detected above the indicated LOQ.
Maximum concentrations shown in
bold and italic font
005-01rptdoc
Page 54

 
TABLE 7-5
Summary of Appendix IX Organic Constituents Detected
MTR Landfill Leachate - Secondary (T-324)
Shell Oil Company
Deer Park, Texas
Sample ID:
T324-1
T324-2
T324-3
T324-4A
T324-4B (Dup)
Units:
(mg/L)
(mg/L)
(mg/L)
(mg/L)
(mg/L)
Sample Collected:
(6/11/2002)
(9/4/2002)
(10/14/2002)
(10/24/2002)
(10/24/2002)
Appendix IX Volatiles
Acetone
0.020 B
0.020
<0.010
0.070
0.090
Benzene
<0.005
0.006
0.014
<0.005
<0.005
Ethylbenzene
<0.005
0.005
<0.005
<0.005
<0.005
1,2-Dichloroethane
<0.005
<0.005
0.014
0.017
0.018
Xylenes
<0.015
0.033
<0.015
<0.015
<0.015
Methanol
<2.5
<2.5
<2.5
<2.5 (a)
4.8
Appendix IX Semivolatiles
4-methylphenol (p-cresol)
<0.010
<0.0075
<0.0015
<0.0015
0.00414
Naphthalene
<0.010
0.0241
0.0125
<0.002
0.01173
2,4-Dimethylphenol
<0.010
0.0222
<0.0015
0.00166
<0.0015
Phenol
<0.010
<0.0075
0.0106
<0.0015
0.01177
Acetophenone
<0.010
<0.0075
<0.0015
0.00181
<0.0015
Phenanthrene
<0.010
0.0574
0.0051
<0.0015
0.00242
Fluorene
<0.010
0.0288
0.00246
<0.0015
0.00189
Bis(2-ethyhexyl)phthalate
<0.010
0.027
<0.0025
<0.0025
<0.0025
Acenaphthene
<0.010
0.024
0.00277
<0.0015
0.00244
Appendix LX
Organochlorine Pesticides
Aldrin
<0.00005
<0.00005
<0.00005
<0.00005
<0.00005
alpha-BHC
<0.00005
<0.00005
0.000576
0.000143
0.000219
beta-BHC
<0.00005
<0.00005
<0.00005
<0.00005
<0.00005
ganuna-BHC (Lindane)
<0.00005
<0.00005
<0.00005
<0.00005
<0.00005
delta-BHC
<0.00005
<0.00005
0.000603
0.000076
0.000106
Chlordane
<0.00005
<0.00005
<0.00005
<0.00005
<0.00005
alpha-Chlordane
<0.00005
<0.00005
<0.00005
<0.00005
<0.00005
gamma-Chlordane
<0.00005
<0.00005
<0.00005
<0.00005
<0.00005
4,4'-DDD
<0.0001
0.0016
0.00024
<0.0001
0.00013
4,4'-DDE
<0.0001
<0.0001
<0.0001
<0.0001
<0.0001
4,4'-DDT
<0.000
<0.0001
<0.0001
<0.0001
<0.0001
Dieldrin
<0.0001
<0.000
<0.0001
<0.0001
<0.0001
Endosulfan I
<0.00005
<0.00005
<0.00005
<0.00005
<0.00005
Endosulfan II
<0.0001
<0.0001
<0.0001
<0.0001
<0.0001
005-0 I rpt.doc
Page 55

 
Table 7-5
(Continued)
Sample ID:
T324-1
T324-2
T324-3
T324-4A
T324-4B (Dup)
Units:
(mg/I-)
(mg/L)
Ong/14
(mg/L)
(mg/L)
Sample Collected:
(6/11/2002)
(9/4/2002)
(10/14/2002)
(10/24/2002)
(10/24/2002)
Endosulfan sulfate
<0.0001
<0.0001
<0.0001
<0.0001
<0.0001
Endrin
<0.0001
<0.0001
<0.0001
<0.0001
<0.0001
Endrin aldehyde
<0.0001
<0.0001
<0.0001
<0.0001
<0.0001
Heptachlor
<0.00005
<0.00005
<0.00005
<0.00005
<0.00005
Heptachlor epoxide
<0.00005
<0.00005
<0.00005
<0.00005
<0.00005
Methoxychlor
<0.0005
<0.0005
<0.0005
<0.0005
<0.0005
Toxaphene
<0.005
<0.005
<0.005
<0.005
<0.005
Kepone
<0.0025
<0.0025
<110025
<0.0025
<0.0025
Appendix IX
Organophosphorus Pesticides
Dimethoate
N/A
<0.0019
<0.0019
0.004
<
<0.002
Disulfoton
Famphur
N/A
N/A
<0.0019
<0.0019
<0.0019
<0.0019
<0.002
<0.002
<0.002
<0.002
Methyl parathion
N/A
<0.0019
<0.0019
<0.002
<0.002
Ethyl parathion
N/A
<0.0019
<0.0019
<0.002
<0.002
Phonate
N/A
<0.0019
<0.0019
<0.002
<0.002
Sulfotepp
0,0,0-
N/A
N/A
<0.0019
<0.0019
<0.0019
<0.0019
<0.002
<0.002
<0.002
<0.002
Triethylphosphorothioate
Appendix IX Herbicides (all non
dectects)
2,4-D
<0.001
<0.001
<0.001
<0.001
<0.001
2,4,5-TP
<0.001
<0.001
<0.001
<0.001
<0.001
2,4,5-T
<0.001
<0.001
<0.001
<0.001
<0.001
.
Appendix IX PCBs (all non
detects)
Arochlor 1016
<0.001
<0.001
<0.001
<0.001
<0.001
Arochlor 1221
<0.001
<0.001
<0.001
<0.001
<0.001
Arochlor 1232
<0.001
<0.001
<0.001
<0.001
<0.001
Arochlor 1242
<0.001
<0.001
<0.001
<0.001
<0.001
Arochlor 1248
<0.001
<0.001
<0.001
<0.001
<0.001
Arochlor 1254
<0.001
<0.001
<0.001
<0.001
<0.001
Arochlor 1260
<0.001
<0.001
<0.001
<0.001
<0.001
Appendix IX Dioxins/Furans
2,3,7,8-TCDD Equivalent 3.79E-09
9.40E-09
?
7.05E-09 3.67E-09
3.66E-09
Notes:
<01 = Not
detected above the indicated LOQ.
Maximum concentrations shown in
bold and italic font
(a)
The original value was 7.6 mg/L. The MS/MSD samples showed high percent recoveries indicating this value may
be biased high. The data shown is for a resample collected December 23, 2002 per EPA's consent.
(b)
B = detected in blank. Sample concentration less than five times the blank concentration.
005-0 I rpt.doc
Page 56

 
TABLE 7-6
Summary of Appendix IX Metals Results
MTR Landfill Leachate - Primary (T-323)
Shell Oil Company
Deer Park, Texas
Sample ID:
Units:
Primary Leachate Tank (T-323)
T323-1
pH 2
(mg/L)
T323-1
pH 7
(mg/L)
T323-1
pH 9
(mg/L)
T323-2
(mg/L)
T323-3
Ong./14
T323-4
(mg/L)
Sample Collected:
6/11/02
6/11/02
6/11/02
8/1/02
9/6/02
9/27/02
Appendix IX Metals
I
Antimony
Arsenic
<0.05
<0.010
<0.05
<0.010
<0.05
<0.010
<0.05
0.0295
<0.05
0.0148
<0.05
<0.05
Barium
0.119
0.120
0.025
0.237
0.108
0.072
Beryllium
<0.005
<0.005
<0.005
<0.010
<0.005
<0.005
Cadmium
<0.005
<0.005
.
<0.005
.
<0.01
.
0
<0.005
<0.005
Chromium
<0.010
<0.010
<0.010
0.014
<0.010
<0.010
Cobalt
<0.010
<0.010
<0.010
NA
<0.010
0.016
Copper
<0.010
<0.010
<0.010
NA
0.025 B
0.022 B
Lead
<0.003
<0.003
.
<0.003
.
<0.010
.
<0.003
<0.015
Mercury
<0.0002
<0.0002
<0.0002
<0.0002
<0.0002
<0.0002
Nickel
0.116
0.112
0.130
0.285
0.00693
0.906 (a)
Selenium
0.008
0.0082
0.0076
0.015
0.0086
<0.025
Silver
<0.01
<0.01
<0.01
NA
<0.01
<0.01
Tin
<0.02
<0.02
<0.02
NA
<0.02
<0.02
Thallium
<0.030
<0.030
<0.030
<0.003
<0.003
<0.03
Vanadium
0.036
0.034
0.041
0.113
0.063
0.046
Notes:
<#4# = Not detected above the indicated LOQ.
Maximum concentrations shown in
bold and italic font.
(a)
The original value was 2.86 mg/L. Nickel was also detected in the method blank. Due to the anomalous
high nickel value, a resample was collected on December 23, 2002 per EPA's consent. The data shown is
for the resample.
(b)
B = detected in blank. Sample concentration less than five times the blank concentration.
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TABLE 7-7
Summary of Appendix IX Metals Results
MTR Landfill Leachate - Secondary (T-324)
Shell Oil Company
Deer Park, Texas
Sample ID:
Units:
Secondary Leachate Tank (T-324)
T324-1
pH 2
(mg/L)
T324-1
pH 7
(mg/L)
T324-1
pH 9
(mg/L)
T324-2
(mg/L)
T324-3
(mg/L)
T324-4A
(mg/L)
T324-4B
Dup
(mg/L)
Sample Collected:
6/11/2002
6/11/2002
6/11/2002
9/3/2002
. (10/14/02)
(10/24/02)
(10/24/02)
Appendix IX Metals
Antimony
<0.050
<0.05
<0.05
<0.05
<0.05
<0.05
<0.05
Arsenic
Barium
<0.10
0.010
<0.010
0.097
<0.010
0.040
<0.010
0.114
<0.010
0.199
<0.010
0.313
<0.010
0.326
Beryllium
<0.005
<0.005
<0.005
<0.00
<0.005
<0.005
<0.005
Cadmium
<0.005
<0.005
<0.005
<0.005
<0.005
<0.005
<0.005
Chromium
Cobalt
<0.010
0.032
<0.010
0.052
<0.010
<0.037
<0.01
<0.010
<0.010
0.043
<0.01
<0.01
<0.01
<0.01
Copper
Lead
<0.010
<0.003
<0.010
<0.003
<0.010
<0.003
<0.010
<0.003
0.08
0.0083
0.014
<0.003
0.011
<0.003
Mercury
<0.0002
<0.0002
<0.0002
<0.0002
<0.000
<0.0002
<0.0002
Nickel
0.113
0.118
0.11
0.055
0.414
0.095
0.080
Selenium
0.0078
0.0083
0.0081
<0.005
0.0053
<0.005
<0.005
Silver
<0.010
<0.010
<0.010
<0.010
<0.010
<0.010
<0.010
Thallium
<0.030
<0.030
<0.030
<0.030
<0.030
<0.030
<0.030
Tin
<0.020
<0.020
<0.02
<0.020
<0.020
<0.020
<0.020
Vanadium
0.031
0.032
0.033
0.038
0.130
0.040
0.030
Notes:
<## =
Not detected above the indicated LOQ.
Maximum concentrations shown in
bold and italic font.
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8.0 DATA EVALUATION USING
EPA
DRAS
In accordance with EPA Region 6 requirements the analytical data for the samples were input
into the Delisting Risk Assessment Software (DRAS), Version 2.0 for evaluation. This
software program provides a scientifically defensible means to evaluate whether a RCRA
listed waste qualifies for delisting under 40 CFR §260.20 and 260.22 with regard to toxicity.
The program calculates carcinogenic and non-cancer risks associated with disposal of a
petitioned waste to a landfill or surface impoundment. For the Shell Oil evaluation, a surface
impoundment scenario was used since the
Landfill Leachate
will be treated in an
impoundment, once delisted. The methods used to calculate chemical concentrations in
media at the point of exposure are based on EPA's fate and transport mechanisms. The
methods used to determine risk associated with the Waste disposal scenarios evaluated for
delisting a petitioned waste are based on EPA's risk assessment algorithms.
8.1 INPUT VALUES
In accordance with the EPA RCRA Delisting Technical Support Document, the following
waste specific information was entered for the DRAS evaluation for both the primary and
secondary leachate:
waste volume: 14,000 tons/yr = 16,619 cy/yr (See Section 3.3)
waste management unit: surface impoundment
maximum concentration of VOAs detected
(Table
7-4, primary and
Table 7-5,
secondary)
maximum concentration of semivolatiles, pesticides, herbicides, PCBs, dioxins
detected
(Table
7-4, primary and Table 7-5, secondary)
maximum concentration of metals detected
(Table 7-6,
primary and
Table
7-7,
secondary)
acceptable cancer risk of 10-5
acceptable hazard index of 0.1
multi-year delisting (default of 20 years)
The concentration data were entered as a "total" basis and TCLP basis since the waste
streams are aqueous. Per EPA Region 6 instructions, the detection limit was entered for
those constituents reported as below the detection limits. A separate DRAS run was
performed for the primary and secondary leachate. The output files from the DRAS runs are
presented in
Appendix F
and discussed below.
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