BEFORE THE ILLINOIS
POLLUTION CONTROL BOARD
STRICT OF
1
DECATUR,
Petitioner,
PCB
(Variance - Water)
ILL
PROTECTION AGENCY,
Respondent.
TAL
NOTICE OF FILING
Illinois Pollution Control Board
100 W. Randolph Street
Chicago, Illinois 60601
with the Office of the Clerk of
the Illinois
KATHER
LURKINS,
etfully s ubmitted,
E
CATUR
Dated: June 15, 2009
By: /s/Katherine
Katherine D. Hodge
Lauren
C.
Lurkins
HODGE DWYER & DRIVER
3150 Roland Avenue
Post
Office
Box 5776
62705-5776
(217) 523-4900
T HIS FILING SUBMITTED ON
RECYCLED PAPER
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
BEFORE THE ILLINOIS POLLUTION
CONTROL BOARD
v.
Respondent.
DISTRICT
OF
Petitioner,
ENTRY OF A
OF KATHERINE
D. HODGE
NOW COMES Katherine D. Hodge, of the law firm
HODGE DWYER &
ER, and hereby enters her appearance
in this matter on behalf of Sanitary District
of
Decatur.
2009
3150 Roland Avenue
Post Office Box 5776
llinois
(217) 523-4900
By: /s/Katherine D. Hodge
Katherine D. Hodge
S DOD-00 ITifingsTOA - KDH
L
TROL BOARD
SANITARY DISTRICT OF
}
DECATUR,
}
}
Petitioner,
}
}
PCB
(Variance - Water)
}
Respondent.
}
ENTRY OF APPEARANCE
OF LAUREN C. LURKINS
N OW CO
k
ins, of the law frtn HODGE DWYER &
by enters her appearanc
of Decatur.
Dated: June
matter an behalf
of Sanitary
District
submitted,
By /s/Lauren C. Lurkil
Past Office Box
5776
linois 62705-5776
217}
523-4900
S DOD-00 ITilings\EOA
- LCL
BEFORE
THE ILLINOIS POLLUTION
CONTROL BOARD
SANITARY DISTRICT OF
DECATUR,
Petitioner,
PCB
ILLINOIS ENVIRONMENTAL
AGENCY,
Respondent.
ITION FOR
VARIANCE
N OW COMES the Sanitary
a ttorneys, HODGE DW
of Decatur ("District"), by and through its
ER, and, pursuant to Section 35(a)
of the
Illinois
415 ILLS 5135 a), and
Part 104 of Title 35 of the
Code, 35 Ill. Admin. Code
§
104. 100 et sec ., hereby petitions the
Illinois
Pollution Control Board ("Board") for a variance authorizing
continued
rges of nickel and zinc, from its wastewater
treatment plant ("Main
Sangamo
Pet
suant to the terms and conditions outlined in this Petition
for
rant it a five-year
variance to
allow it
time to continue its evaluation
of the
issues
a
solutions regarding
its nickel and zinc d
invest
's variance request
stems
from the Board's adoption of more stringent nickel
and zinc water quality standards,
which at the time,
were
not
anticipated to adversely impact any
gers.
al Pollutant Discharge
Elimination System
") permit was renewed, the Illinois
Environmental Protection Agency ("Illinois
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
EPA" or "Agency") imposed
new effluent limits for
stringent standards.
Since the District
water within Lake Decatur for
the City of Decatur's water
supply, du
rict's
effluent limits directly reflect
the water quality standards,
there are times
when there may be no discharge
downstream to the
Sangamon River into
which the District discharges.
As a result, the District could not
be granted a mixing
zone, and t
Although the District undertook immediate
action to
nd Company ("ADM"),
one
kel and zinc in its
discharge and to investigate compliance
options, the District
could
not
design, permi
chase, construct
and commence operation of any
adequate
rdance
wit
and zinc to meet
the more
s located
downstream of the
dam that reta
compliance schedule
set forth
detailed
herein. Similarly, Archer Daniels
M
weather,
of the District's most
significant
ributor to nickel
and zinc
loa
ommence
dentify
the sources of the
Further, human
hea
mpliance
antrng of this variance since the
amount of nickel and zinc to
be discharged
would not increase
beyond historical levels. This variance
is necessary far the District to
ions.
HICH VARIANCE
IS SOUGHT
The District is seeking a five-year
quality standards for nickel
and zinc, w
Board
rules and from 35
based effluent limits.
sped to the general
use water
hich are set forth in
Section 302.208(e) of the
de § 304.105 as it applies to establishing
water
The
water quality standards for nickel
and zinc are defined
2
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
in terms of conversion factor multipliers
for dissolved metals. See 35 1.11. Admin.
Code
302.208(e).
The acute standard ("AS") for nickel (measured
as microgram
is
defined
as follows:
eA
+BIn(H)
x
0.998 *,
ter ("fig/L"))
where:
A =
0.5173
B = 0.8460
ex = base
of
natural
logarithms raised to the x-power
In (H) = natural logarithm of Hardness (STORET
00900)
* = conversion factor multiplier for
disso
(measured as wg/L) is defined as follows:
e
A +Bln(H)
x
0.997
where:
A = -2.286
B =
0.8460
Id.
= natural logari
multiplier for dissolved
metal
The AS for zinc (measured as pg/L) is defined as follows:
B In
H ) x 0.978 *,
where:
A =
0.9035
B = 0.8473
e-' = base of natural logarithms raised to the x-power
In (H) = natural logarithm
of Hardness (STORET 00900)
ersion factor multiplier for
I d.
The CS for zinc (measured
as pg/L) is defined as follows:
B ln(H)
X 0 .986*,
where:
A = -0.8165
B =
0.8473
ex = base of natural
logarithms raised to the x-power
In (H) = natural logarithm of Hardness
(STOFLET 00900)
* = conversion
factor multiplier for dissolved metals
I d.
The AS
for both nickel and zinc "shall not
be exceeded at any time," except as
provided in Section 302.208(4
nickel an nc
"s
. 3 5 Ill. Admin. Code 02.208(a). The
CS for both
be exceeded by the arithmetic average
of at least four
Ilected
over any period of at least four days," except as provided
tion
302,208(d). 35 Ill. Adm
(d)
.208(4) provides as follows:
1)
roved
a zo
.1
eeeded in any waters
except
allowed pursuant to Section
302.102, the
The
CS shall not be exceeded outside of waters
is allowed pursuant
to Secti
3) The [human health standard] HHS shall not
be exceeded
outside of waters in which mixing is allowed pursuant
to
Section 302.102.
35 Ill. Admin.
Code § 302.208(4).
ict is also seek g a variance from
the rule establishing the methodology
ent limits at Section 304.105
of the Board rules.
35 1.11. Admin.
Code § 304.105.
04.105 provides as follo
In addition to the other requirements
of this Part, no
effluent shall, alone
or in combination with other
sources, cause a violation
of any applicable
water quality
standard. When the Agency
finds that a discharge
which
would comply
with effluent standards contained in
this Part would cause
or is causing a violation of water quality
standards, the Agency
shall take
appropriate
action under Section 31
or Section 39 of the Act to require
the
discharge to
meet whatever effluent limits
are necessary to ensure
compliance with the water
quality standards. When
such a violation is
caused by the cumulative effect
of more than one source,
several sources
may
be joined in an enforcement
or variance proceeding, and measures
for
necessary
effluent reductions will be determined
on the basis of technical
feasibility, economic reasonableness
and fairness to all dischargers.
35 Ill. Admin.
Code § 304.105.
e Board to o
nois EPA, pursuant
to
309.184 of the
Board rules, to modify the District's NPDES
p
s:
by the CWA and the Ac
request
ed by these
uld impose
an
e hardship
on the app
Iicýint
or permittee. Any
in 6iceoýrdance
with Section
104.101 and Part 104
shall govern the proceeding. If such
a variance is
granted the Board shall order the Agency
to issue or modify an NPDES
Permit
consistent with the Board Order, the
CWA, Federal
Regulations and
the Act.
(Note: Prior to codification, Rule
401 and Part
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
11.
A. The District
lant and Operations
Description
The District, located in Macon
County, Illinois, is engaged in the treatment
of
domestic and industrial wastewater
for the City of Decatur, the Villages
of Forsyth and
Mt. Zion, and for industrial and commercial users in
the Decatur, Illinois, metropolitan
area. The District employs approximately
61 full time employees, and was formed in
1917. The original Main Plant, located at 501 Dipper
Lane, Decatur, Illinois, was
924. Major
expansions and plant upgrades were made in 1928, 1957,
1964 and 1976, and the current plant was completed in 1990. The Distric
s
ly 90,000 residents of
the City of Decatur and the Villages of Forsyth and
Mt. Zion, and 26
sign
industrial and commercia
An average of appro
S .
M ain Plant consists of screening,
maximum
flow of 125.0 MGD. Treatment at the
sludge, secondary clarification, disinfection,
dechlorination,
anaerobic digestion, flotation
thicken ng, and land application
-stage activated
to surface water,
Judge on area farmland.
ategorical SIUs and 9
Receiviniz Waterway
nd more than 1,000 other
ain discharge is via Outfall 001 to the Sangamon River
at 39°
49' 56" North Latitude, 89° 0' 7" West Longitude. At the discharge point,
the Sangamoi
6
R
esignated
as a General Use Water under
Section 303.201 of the Board's
rules.
As discussed above, the general use
water quality standards for nickel
and zinc are set
in Section
302.208(e).
The segment o
on River that receives discharge from
the Main Plant
ID
IL-E-09) is listed on Illinois' 303(d)
list of impaired waters for
2008.
See Partially Approved 2008 Illinois
303(4) List at 54, available at
http://www.epa.gov/regions/water/wshednps/pdf/att
3 partial_approval_final.pdf.
The
for this segment are aquatic life, fish
consumption and primary contact
potential causes
of
impairnient
given for the segment are
manganese,
yls and fecal
coliform. Id. The potential
sources associate
s5
y/road/bridge
runoff (non-construction related), crop production
(crop land or dry
land), agriculture, urban
*f/storm sewers and
source unknown. See Appendix B-2,
ms, 2008 at 1-2 and 87, avai
http://www.epa.state.i1.us/water/tmdl/303-appendix/2008/appendix-b2-streams.pdf,
C.
Tire District's
Current NPDES Permit
The District holds an NPDES pe
which became e
y Illinois
EPA on April 20, 2007,
2007, and
expires on June 30, 2012, a copy of which is
ins effluent limits for nickel
and z
calculated in accordance with the formulae set forth
08(e). The
ted effluent concentration limit for nickel is 0.011 milligrams per liter ("mg/L")
;
a monthly average with no daily maximum concentration
limit. The permitted effluent
concentration limit
for zinc is 0.046 mg/L as a monthly average
and 0.258 mg/L as a
daily maximum.
According to an Illinois
EPA memorandum regarding the water quality based
rict's permit, the nickel and zinc
standards were "based on
hardness data
collected at AWQMN station E-05, Sangamon River, SE of Niantic, with a
/L as CaCU3." Illinois EPA
Memorandum from S.
Hah.n regarding Water Quality Based Effluent
Limits, Decatur Sanitary
District,
NPDES
#IL0028321 (Macon County) (November 9, 2006), attached hereto as
In
addition,
pursuant to Special Condition 17 of its NPDES permit, the District
anslator Study, the main reference for which was "The
Metals
Translator.
ted States Environmental Protection Agency ("USEPA"), EPA823-B-96-007, June
discusse
dvised the District that, based on the Translator Study, the permit limits
Recoverable Permit
Limit from a Dissolved Criterion,"
her 20, 2007, as part of
t forwarded this Translator
ore detail below and which is attached hereto as Exhibit C. Subsequently,
ed to 0.015 mg/L
for zinc. See email from
S.
Twait at Illinois
monthly average) for nickel and 0.075 mg/L (monthly
average) and 0.416 mg/L (daily max
e at the District (January 2, 2008
d
hereto
as Exhibit D.
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
The
for ach
ES permit
also includes at Special
Condition 18 the following
schedule
liance with the above-mentioned
effluent
im Report on
effluent and
f; months
from the effective
stream sampling to date and
date of this Permit
what measures
are necessary to
ith Final Nickel
and
itations
(2) Interim Report
12
months from the effective
date of
this Permit
Interim Report
18
months from the effective
date of this
Permit
(4) Permittee
Achieves
24
months fro
Comp
and Zinc Effluent Limitations
ber 20, 2007.
See Exhibit C. The Second
d ate
of thi
a ttached hereto as follows:
The First Interim Report
was submitted to
ois EPA on
on December
29, 2008, and is
attached hereto
as Exhibit F. Thus, the current deadline
for compliance with the nic
and zinc limits
in the District's NPDES
permi
of the water quality standards
for both nickel and zinc in the segment
of the Sangamon River to which
the District
harges, the
established
in the District's NPDES
permit, as well as the associated
compliance
schedule.
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
Prior Variance(s) Issued to the District
or Any? Predecessor Re2ardin
Neither the District, nor any of its predecessors, has
regarding relief that
Similar Reli
District
of Decatur's Sewage Treatment Plant into the Sangamon
River, Macon
County,
Illinois.
However, on January 22, 1987, the Board granted the District
a
for variance
g it from 35 Ill. Admin. Code § 304.120(c),
which, at that time, limited
discharges
from the Districts Main Plant to 10 mg/L of five-day biochemical oxygen
demand ("BOD5") and 12 mg/L of suspended solids. Final
Opinion and Order of the
Board, In the Matter of.
Site-Specific Rulemaking for the Sanitary District of
Illinois, R85-15
Code
y 22, 1987). The Site-Specific
ilar
to what is requested in this Petition.
nd provides the following:
from the Sanitary
b)
The provisions of Section 304.120(c) shall not apply to said
discharges, provided that
said
discharges
shall not exceed 20 mg/1
biochemical oxygen
0) and 25 mg/1 of total suspended solids (STORPT
. Code § 304.212.
While
th
atur,
Rule is not
a variance and does not
discharge.
sed in this Petition, it is relevant for de
sly granted the District regulatory relief for its Main Plant
effluent
10
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
E.
Nature and Amount of Materials
Used In Activity for Which
ought
The District
provides treatment for wastewater
received from domestic,
ial and industrial sources. During
dry weather, two industrial
users, ADM and
Tate & Lyle Ingredients
Americas, Inc. ("Tate
&
Lyle"),
provide approximately 50
percent
of the wastewater flow received by
the District. The District conducts
an
ratory analysis program to monitor industrial
sources,
wastewater entering the treatment plant,
the treated discharge to the Sangamon
River and
other locations.
nitoring
program, the District has identified
sources of
nickel and zinc
in the incoming wastewater.
locations in the collection
system
ly
domestic and commercial wastewater has
indicated concentrations below
the laboratory detection limit. Average industri
ADM
9.403 pounds per day (0.102 mg/L)
0.351 pounds
per day (0.010 mg/L)
0.034 pounds per
day (0.006 mg/L)
egard to zinc, small amounts
are present in domestic and comme
wastewater,
although the majority of the Dist
follows:
like other
31.446 pounds per
day (0.319 mg/L
Tate & Lyle
4.487 pounds per day (0.124
mg/L)
All other industries
1.281
pounds per day (0.226 mg/L)
Domestic and commercial 7.507 pounds
per day (0.052 mg/L)
des
physica
load is from industry,
reatment
facilities,
and. biological treatment processes.
While specific treatment processes
for metals removal are not provided,
significant incidental removal of metals from
the
II
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
wastewater does occur. The District's removal efficiency is approximately
53 percent for
nickel and 77 percent for zinc.
The District regulates incoming wastewater constituents by ordinance, including a
pretreatment ordinance adopted pursuant to its 1`d'DBS
permit requirement to implement
an industrial pretr
with the
program.
The ordinance limits are incorporated into discharge
ed by the District to SIUs. Both ADM and Tate
&
Lyle
are in compliant
r current
ge permit limits for nickel and zinc.
mount of Discharges of Nickel and Zinc
Currently
Generated By the Activity
to the reissuance of th
ed its treated discharge and the Sangamon River
upstream ai
pint for nit
i
available in the Sangamon R
dry conditions occurred in
the fal
downstream nickel concentrat
of the
d from 0.01 to 0.03 mg/L during that period,
ods,
However, from December 2007 through March 2009, only one downstream
sample
exceeded the expected water quality standard of 0.015 mg/L. In addition, during the
mpling period, only one downstream sample exceeded the expected
rage concentration and none exceeded the maximum concentration.
Monitoring results from March
2007 through March 2009 are summarized
in the
table below.
ýangamon
River approx. 2
miles
downstream
of
007 reissuance of the NPDES
permit. the
t l i
ained
therein,
compliance by July 1, 2009. As
soon as the permit became
ions of several alternatives including reduction
of
ough the existing industrial pretreatment
program, potent
adjustments to the permit limits (including
the Translator Study), and treatment
13
technology that could potentially
be employed to improve removal
at the District's
Plant.
The District has calculated tentative
pretreatment local limi
enable its
discharge to meet its current
NPDES permit limits. These
calculations were performed
following
USEPA, Region S guidance and have
formed the basis for discussions
with
reasons.
to & Lyle. The
District considers these numbers
to be tentative for several
the calculations are based on limits
in the District's April 20, 2007
s discussed further
below, revised permit limits
based on the
ator
Study
cently been included
in a proposed modified
dition, the District has
made a substantial effort to idet
that could arise
concerning alloc
lementation
of the limits. Finally, it has
been the
order to assure
camp
pliance schedule for nickel
contained in its
iicant changes to treatment processes
or operations. W
regard to treatment at the District's Main
Plant, any treatment process would need
to be
dle
at
least
the design average flow of 41 MGD,
and potentially the design
0
concentrations of metals
from such streams as electrop
ies for removing relatively
high
wastewater are well-
s limited by the very
low concentrations in the District's
14
wastewater
stream. For example, precipitation as
1 hydroxide is
one technology for
removing nickel from a solution. However, the solubility
of nickel hydroxide at the high
pfl level required
(pH 10 - 11) is approximately 0.12 mg/L, nearly an order of magnitude
effluent limit. Even under ideal conditions,
precipitation could
not achieve the limit.
Another common metals removal technology, filtration, would not
effectively
the D
ci
,trict's effluent. Mechanisms for improving
the incidental removal of metals
1 wastewater treatment plants vary depending on whether the metal
species is
particulate or dissolved (either as a metal ion or a metal
complexed with another
1 of particulates or dissolved metals adsorbed onto particulates
ed sludge floc) can potentially be improved by effluent filtr
sand or other
of effluent ni
Id not be removed by
Add-on chemical treatment technologies, such as ion exchange and reverse
osmosis, would be expected to remove dissolved nickel from the District's Main
Plant
. Both treatment technologies remove metals from the bulk effluent flow stream
and concentrate them into a smaller volume, high concentration stream
that
requires
further management. Both also require significant
operating costs for energy, labor, and
me
osmosis
(ion exchange).
The consulting firm
ided the District with a
istrict's
effluent, however, shows
of $4 per gallon per day capacity for reverse osmosis
treatment, not considering the cost of brine disposal and operating costs. At a
minimum,
15
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
appro
ly 2 5 MGD
tment system, perhaps by half.
However,
a
roposed permit limit of 0.016 mg/L, resulting in a minimum capital
cost of $100
million,
not considering brine disposal. A brine disposal system could double the capital
cost. This exceeds the construction cost of the District's entire plant, to achieve
a
removal of approximately
six
pounds
per day or
less
of
nickel
from the effluent.
In general, the capital cost of an ion exchange system would be expected to total
less than that of a reverse osmos
substantia
ch would be required to find an ion exchange resin suitable
for removing nickel that is likely to be in a complexed form in the District's
effluent.
lso depend on the removal efficiency that could be achieved,
ould
ndus
Regardless of the treatment technology con
1 cost. For
would need to be treated to meet the
al of nickel at the
Id minimize the volume of water to be treated and, therefore, the
he nickel limit on working with in
n, the District
ADM as the largest industrial. discharger o
calculated pretreatment local li
1 users and, in particular,
kel to its system. The District has
I
ischarge to meet its current
limit for
total
nickel from AD
day. ADM's current loc
of 15.6 pounds
mg/L dissolved nickel, correspon
day at a flow rate of I
pounds per
a loading
MGD. Based on
sampling
from
January 2008
through April 2009, ADM discharged an average of 6.382 pounds per day of dissolved
nickel and 9.403 pounds per day of total nickel. ADM would need to reduce its nickel
16
discharge to the District by nearly two-thirds in
order for the District to meet its NPDES
gations of nickel
reduction alternatives are discussed further
below.
Compliance with the Zinc NPDES_ Permit Limit
Cannot Be Achieved
By
the Compliance Date
The District also cannot meet the compliance
schedule for zinc contained in
out significant
changes to treatment processes or operations.
Treatment options for z
the District's Main Plant are the same
as described above
for nickel. The District has also calculated
pretreatment limits which would need to be
used on industrial users
to enable the District's discharge to meet permit limits.
However, the situation
ndustrial zinc sources
and control is quite different from
with nickel. Through discussions
with ADM and Tate & Lyl e, the District found that
er treatment chemicals were in use at
both facilities and were
the largest source of zinc in the District
cooling tower treatment programs.
Both industrial users have
riot
p ounds per day at
ed maximum is 88.97 pounds
per day. Based on samp
2008 through April 2009,
ADM discharged an average of 34.351 pounds
per day and a maximum of 81.908 pounds per day of zinc. Eight
of 18 samples exceeded
the average limit.
As noted above, effluent monitoring indicates that the District's discharge
is
pliance with the proposed NPDES zinc
average limit during the major
of sampling events. However,
additional time is needed to address several concerns
with
consistently achieve this limit. As
discussed in detail below, ADM is
management alternatives to determi
bether it can meet the District's tentative
g operation of its wastewater treatment plant ("WWTP") and in particular, solids
pretreatment local limit under all conditions.
Also, two new industrial facilities that will
discharge wastewater to the District's Main Plant are currently in the design phase. A
0
of these proposed wastewater streams
would consist of coo
blowdown streams and while the District would closely regulate any zinc-based cooling
tower treatment additives, any background zinc concentrations
would increase through
the cooling process. Additionally,
time is needed to verify the accuracy of assumptions
requ
ocal limit development process,
various industrial
users
and, in
the case of zinc, a very high (greater than 90 percent)
projected removal rate by the District's treatment process.
Based on samples taken by ADM since January 1, 2009, ADM would
be able to
to meet the proposed limit is almost solely based on the
amount
could achieve compliance with its zinc allocation (at least much of the
rough reduced sludge wasting. However, this would be only a very
short term
solution. The reduction of sludge wasting would cause the sludge to build up w
pretreatment system and cause major disruptions
within
a rn
likely compromise
the
District
to properly operate its Main Plant. To counteract
18
ids would carry over with their effluent to the District. These
solids would
ncluding allocation assumptions for
erobic portion
of the system
eeks. At that point, significant and uncontrollable amounts of
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
the solids "carry over," the volume through ADM's WWTP
would have to be reduced.
To that end, major
The
Distri
ions of
could not be restarted until a sludge removal and drying system could be
design, pe
. The
construction of such a system would be very costly and would
likely
take more than a year.
C .
The
's Decatur Complex would have to be shut down and
orts to Identify Compliance Options
s first effort toward compliance was to complete the Translator Study
tioned above. The work on the Translator Study started in March 2007,
prior to the
permit issuance
in April 2007, and continued through November 2007. As the
Study progressed, the District determined that it would provide very little relief. The
07, as part
4-5 of Exhibit C for the proposed nickel and
ted in
e data.,
ial samples, the District's effluent samples and stream sampling
compiled, which showed that the source of nickel in the District's
flow, and the most s
Also, w
including ADM and Tate & Lyle, in August and September 2007, to discuss
industrial flow from
both
ADM
and
Tate
&
Lyle. T
nickel and zinc
District's new ni
nd zinc limits at those meetings. The District then met with
0,
2007, to discuss the
situation.
Please
see
the
summary of
. Personnel from ADM and Tate & Lyle were made aware
of the
ranslator
Study.
sample data that was given to Illinois EPA personnel during the October 30, 2007,
19
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
meeting, attached hereto
as Exhibit G. During that meeting,
Illinois EPA advi
extend the compliance
schedule in the permit
was premature, but
could be considered at a later date.
Since the District's meeting with Illinois
EPA, the District has made
significant
efforts to identify treatment options
regarding its nickel and zinc
recommended
by
Illinois
EPA, the District discussed
options for reducing nickel and z
loadings
wi
pretreatment
zinc.
e rous discussions
with the industries during 2008,
ate & Lyle. In
early 2008, the District calculated
new local
its
that would allow it to meet the upcoming effluent
limits for nickel and
These proposed limits were provided
to ADM and Tate & Lyle and
were the basis
Report
and indicate
hardness data the District collected
See
not yet
dified to revise the permi
mon
Also
in January 2008, the District a
am Plant.
om both ADM and
it discharges and the
pretreatment
numbers.
ograms, as
. ADM
ned above, and had been
identified as the primary source of nickel; it was used
as a catalyst in
is zinc discharge to meet
the limit,
n reviewing a better control
and monitoring program that
several of its production processes. AD h
ad begun reviewing treatment technology
that
20
would enable it to concentrate
and recover nickel from the wastewater
stream for that
process. ADM's
efforts are continuing, including a recently
completed trial of
electrocoagulation as a nickel removal process.
Unfortunately, it was found that the
process actually increases the nickel
concentrat
used in the rocess.
possibly due
to nickel in the electrode
The District continues
to work with ADM and Tate & Lyle
to meet the nickel and
As discussed further below, during the
December 4, 2008, meeting between
the
2009,
the District submitted its NPDES permit
modification
its NPDES permit to
extend the compliance schedule contained
on April 3, 2009, the District
forwarded
to Illin
Section
the District
attached hereto
as Exhibit H. Therein, Illinois EPA proposed
to
extend
the schedule of compliance for nickel and zinc from
two years to three years.
date of the filing of this Petition,
the modified NPDES permit has not
been issued
Illinois EPA. Also during late 2005, discussions continued
between Illinois EPA, the
M and Illinois EPA, Illinois
EPA recommended that the District
submit an
st. Please see the dis
On May S, 2009,
ADM regarding the best means
to address the District's nickel and
zinc
id not know that achieving compliance
with the nickel
ould be
is NPDES permit, according
to the schedule also contained in the
Ztinuing to operate both facilities
until ADM
21
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
discovered, in mid-2008, that incoming grain was responsible for significant amounts of
provided
the effluent sent to the District. Upon this discovery, the District and ADM
that seeking a variance would also be appropriate in this situation. Because
with available data and a summary of the issue as part of its Third
port. See Exhibit F. In light of this information, Illinois EPA, the
of the complexity of the issues at hand, it has taken time for the District a
coordinate with Illinois EPA and to prepare this Petition. On April 28, 2008, th
ovided a draft of this Petition to Illinois EPA for its review. On May 14, 2009, the
Illinois EPA met to discuss the same.
VI's Efforts to Reduce Its Nickel and Zinc Discharges
s set
tightened nickel
ficant co
ulated from the sampling data, which ADM would be required to comply
with
ADM's Decatur Complex consists of multiple, separate processing plants, which
2008, the District met with ADM and sha
by
July
2009. It was not until this time that ADM first recognized the implications that
Id have on its operations.
a
Corn
n-site
WWTP operated
by
Corn
Plant personnel.
07, the Distract notified
processing plants consist of the
roducts Plant, Cogeneration
ducts, us
cessing Plant, West Soybean Processing Plant, Vitamin E Plant,
t. Each of these unique plants produces
continuous processes, and creates wastewaters
22
which generally are reused multiple
times prior to being discharged
to the WWTP. The
WWTP treats approximately
I l MGD through a newer
anaerobic treatment system
followed by aerobic treatment
prior to discharge to the District.
Due
to the high wastewater flow and very low
concentration of nickel and zinc in
t he final e
a ccomplisl
y of
cats an
Is. Through testing,
ADM was able to
eliminate the incoming
raw water as a source. Further, based
on process knowledge,
1
both i
at the only
source of nickel was nickel catalyst (which is used
0
s.
lant), while the zinc was primarily from
cooling tower wa
be on a "soluble" basis. In May, however, the District, after consultation
with Illinois
nformed ADM that
the
limits
would be on a "total" rather than "soluble" basis.
ble portion of nickel and zinc in ADM's
final
y 25 percent and 75 percent, respectively.
This change in
measurement
basis meant much of the sam
leted was inadequate
to
reach
appropriate conclusions and could not be used for
data comparisons with future data
a "total" basis.
oncluded that reductions
in nickel and zinc would need to
be
Thus, in January 2008, ADM began
identifying possible
tals through complex-wide sampling
and a pre
23
Second, ADM encountered a problem with its sample
analysis procedures. ADM
became concerned that i d ata was not ma
on investigation, ADM
research
laboratory ("ADM Research") determined that the lab syringe filters
used
in
the
alysis contained zinc themselves,
which was leaching into the filtrate. This issue
took several weeks to identify and confirm the filters as the problem. It then took several
additional weeks to find suitable filters to meet the testing requirements.
Spl
for both nickel and zinc
results.
Third, ADM was surprise
ral streams which were
known chemical and processing aids that contained these metals.
arced that soybeans contain approximately 4.1 ppm nickel and
pp
Illinois
EPA approved laboratory to confirm
contains approximately 0.53 ppm nickel and
550,000 bushels of corn and 200,000 bushels of soybeans per
nickel and 25 times more zinc than ADM would be allowed to discharge into
the Decatur Complex comes into the Decatur Complex just through its raw materials.
Other "non-traditional" sources were also identified, such as the 50
percent sodium
co
el, but since the Decatur Complex uses nearly six
s
of sodium
hydroxide
per
month,
the contribution of additional nickel to
the Decatur Complex wastewater system also s
ant.
24
While ADM
first
of
2008,
du
ime, it also began evaluating various means to reduce or
lie
identification of nickel and zinc sources during the
t i the
emphasis began trans
sampling and source identification
to identifying and trial
or eli
e metals. Following are discussions of these activities to date for both zinc
and nickel.
1.
Zinc
As referenced above, the chemicals used in the cooling
tower water treatment
program
were initially identi
cc of zinc in the Decatur Complex
otential methods to reduce
learned that the largest source was the
corn and soybeans
doing so. However, ADM learned t
of zinc containing materials has cease
ccessful in
Plant towers continued to show elevated zinc levels even after
the
a higher pH program in August 2008, which reduced the
ount of zinc leaching from the system. Even so, it was well into the fall before all the
cooling water from
the towers was generally below the zinc targets.
As a result of its efforts to date, ADM has reduced its zinc discharges to levels
that
are generally
less
than
its
allocation.
Further,
potential nickel reduction strategies
discussed below should provide some additional redo
going forward. First, the
ever, there are still two
s ability to consistently ac
ct mixes produced in the Decatur Complex during the
25
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
recent sampling are
ones which would be expected to result in lower zinc
concentrations
than other potential product mixes. Thus, as product mixes
change (e.g., production of
more fructose),
the zinc conce ion may again increase. Therefore, additional ongoing
monitoring of the effluent will be necessary to determine the
impact of these process
variations. The second outstanding
ation of metal sulfides i
bic system, which is discussed in more detail later in this
2.
Nickel
ADM readily identified the use
process and i
ickel catalysts in the Corn Plant's
sorbitol
an Processing Plant as significant nickel
contributors.
ADM had looked at nickel
recovery from the sorbitol process by electroplating in 2006
chnical and economic issues. In
March 2008, the Corn Plant hired a nickel consultant to look
specifically at nickel
sorbitol process. He, too, focused primarily on electroplating.
Unfortunately, a number of problems became apparent, including low nic
the need to use ch
which are non-food grade, and the presence of various other cations and anions.
Once
hat electroplating was not a feasible option.
Next, the Corn Plant began investigat
the sorbitol
stream. However, ADM discovered that gluconic acid present in
the process
forms
a
complex with nickel, which
it from coming out of solution. While that problem
could be solved by oxidizing the organ
ozone
and
hydrogen per
prior to the precipitation,
of extreme amounts of
26
additional
them
Over half of this waste is routed
directly to the WVVTP and cannot be readily
as
unable to provide any other options.
To learn more about the nickel losses in
the sorbitol process, ADM continued its
testing program throughout
the year. One of the consultants ADM involved
in this
project
identified a potential process change to reduce the nickel
through a combination
of water capture and redirection. A trial
of this option was completed in November 2008
positive results.
ADM has begun making the necessary changes
to implement the
option, w
make it infeasible.
ADM also opened a
dialog with the
Ives considerable
piping installations and modifications.
As noted
previously, the sorbitol process is not the only nickel source
in the Corn
Plant: the incoming corn also contains significant
amounts of nickel and zinc. Testing
s, the resulting starch slurry contains nickel.
aterial for many of the downstream
value-added
products, including various sweeteners.
After
change system. As a resu
treated.
about
50 percent of the nickel to precipitate and 85 percent of the zinc,
sting has shown that raising the
pH of the other half of the waste
Id then be removed from the waste stream. Unfortun
uses approximately 3 million pounds
of 35 percent hydrochloric acid a month in
stream,
it would require millions of pounds of sodium hydroxide (which
also contains
nickel) or some other base to raise
the pH of this waste material to 10 for the precipitation
ecipitation option does not appear to be viable.
27
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
ber 2008, Illinois EPA made two suggestions for further
northern
First, it directed
o a nickel-catalyzed hydrogenation
facility in
linois as a possible source of expertise regarding
nickel removal. AD
contacted them and learned that their nickel removal technique is high pH precipitation.
because of their feedstock, they
do not have a problem with nickel -gluconate
complexing. As a result, their treatment system is not transferable
to
ADM's
processes.
Second, Illinois EPA suggested investigating electrocoagulation,
which ADM had not
done.
Samples were sent to an Oregon company for electrocoagulat
nation. Th
tive for nickel and
iekel was confirmed
t electrode
The Oregon company
explanation for t
ADM's East and
a
bean Process
gnificant po
gnificant nickel
atalyst
ping practices were implemented in the spring of 2008,
has been inconsistent, and ADM continues to investigate handling
However,
Processing Plant continues to work with outside contractors and vendors to identify any
other potent
s.
The East Soybean Processing Plant is single largest contributor of nickel in
M's effluent, and all the nickel
is from
the soybeans
processed.
Sampling
at
the East
28
Soybean Processing
Plant has identified four primary
streams containing nickel.
One of
the four
streams, which is also the lowest
flow, contains roughly
half the nickel in the
ast Soybean Processing
is effluent. The East
Soybean Processing Plant is
attempting
to locate a feed or fertilizer
outlet for this wastewater
stream. Further, ADM
Research is assisting the East
Soybean Processing Plant in investigating
any process
nges or unique
nickel removal options
that could be viable for the remaining
three
streams.
Formation
in Anaerobic System
In the spring of 2007, ADM
started up a new anaerobic wastewater
treatment
series with its ex
of the solids and `
ition to improved
owed solids
excess
solids through the
obit
Insoluble
in the sludge. Some o
nto the
aerobic system. This aerobic/anaerobic
sludge is
"wasted" into
the effluent to control the solids in the system. Through
sampling and
the soluble nickel component
this sludge alone, even
is greater than ADM's proposed limit
while the insoluble
rom the sludge could cause the
ded based on the current rate
of
solids "wasting."
iries regarding
the mechanics of metal sulfide formation in
anaerobic systems and has
sought assistance from ADM Research
and CE Betz Company
29
to address
this source of metals.
ADM has learned that
the nickel sulfide formation
mechanism cannot be forced
to a higher degree
of precipitation without raising
operating
pH to a
level which would negate
chemical oxygen dema
have gas formation.
ADM continues to investigate various
combin
reduction
options that have
shown the potentia
eneficial
of technologies
and source
help reduce
the nickel and zinc.
part of this ongoing
investigation, capital and operating
costs associated
with each
technology are being developed.
In addition to cost and technical
feasibility, secondary
higher likelihood
of
success also entail significant
costs and have secondary negative environmental
impacts.
s/Process
Changes ADM Has Implemented
or
Determined
Infeasible
In summary,
to date, ADM has either implemented
the following
technologies/process changes or
dete
viable alternatives
to the nickel catalyst used in two
processes.
d product quality
issues, no other catalysts
etermined to be viable.
Nickel - Ion Exchange
Followed
bv
Nickel Electroplating -
d multiple technical issues
during bench-top testing of
samples, along with the fact that non-food
grade chelating resins
would
be necessary. The option was determined
to not be
lly feasible.
Use of non-food grade chelating re
grade IX waste is acceptable,
but would yield far too low
a nickel
concentration to make electroplating feasible.
- Hick pH Precipitation for
Sorbitol Process - Tests
conducted to determine feasibility
of
precipitating
the nickel were
ineffective
due to a gluconate nickel complex
which prevents
precipitation.
3 0
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
ests showed
only moderate precipitation
efficiency due to the already
low
nickel
concentration. Additionally,
significant quantities of
chemicals
would be required, which makes
the technology
infeasible.
Nickel
- Ooeration Changes - ADM modified
the Sorbitol ion
exchange regeneration
rinse sequence to reduce
nickel discharged
to the WWTP.
6.
Zinc
- Cooling Tower Water Treatment Program
- In the summer
of 2008, ADM
implemented an alternative program at
the Corn
d the BioProducts Plant
that does not contain zinc in the
chemicals.
No other facilities at ADM's Decatur
Complex were
- BioProducts Cooling owe r - In
the fall of 2008, ADM
As set
implemented
a higher pH program to
tower.
leachin from the
inc-based
treatment program.
1. The option was
1 removal
at the al
ion in ADM waste streams.
to shut down much of its Decatur Complex. Moreover, the
District cannot cease
lant, which
provides treatment of domestic and industrial
wastewater
for the City of Decatur, the Villages of Forsyth and Mt. Zion,
and for
ur metropolitan area. ADM also cannot
cease operations
at its Decatur Complex wi
The Distri
2009, unt
requesting
tion
of the local economy.
allowed additional
time, i.e., from July 1,
30,
2014,
to continue its study of all possible compli,
31
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
which may
(OR UNRE
proposes
the compliance plan set forth in Section
VI below.
V.
SONABLE HARDSHIP
Prior to reissuance
of the District's NPDES permit in
2007, the District operated
under a series of permits with no effluent
lim
prior NPDES
permit reissuance in 20
andards adopted by the Board.
istrict's discharge concentration
was, and continues to be, well
below that value. The 2007
reissuance incorporated water quality based
limits based on
the new water qual
rrent NPDES permit effluent li
in
Section 302.208(e
uded in the NPDE
permit, would
1
relief During
this time, the District
for nickel or zinc. At the time of the
1, the water quality standard
for both
the general
use water quality
, according to the compliance schedule
and unreasonable hardship
on
below and which are reflected in the District's permit,
have had
Illinois
EPA, in support of its proposed revised standards in
2001 through 2002,
advised the
are o
have problems complying with the new
water quality standards (which included new
water
quality standards for nickel and zinc). Thus, neither the District nor ADM
knew at
that
i
32
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
lemaking
entitled In the Matter of: Water Quality Triennial
Review:
Amendments to 35
. Code 302.105, 302.208(640,
302.504(a),
302.575 d,3309.141(h), and
Proposed 35 Ill. Ad
d zinc).
304.120
and 309.157, R02-11, Illinois EPA, in part, proposed
to amend the Board's
water quality standards for nickel
and zinc as part of its "triennial water quality standards
review." Illinois
EPA Statement of Reasons, In the Matter of. Water Quality
Triennial
o 35 111. Adm. Code 302.105, 3 02.2
08(e
0 9.141(h); and Proposed 35 1. Adm. Code 30.1.267, 301.313,
301.413,
.267301.313, 301.413,
3 0 2 .504
3
04.120 and 309.157, R02-11 (November 7, 2001). Illinois
water quality sta
protective
of aquatic life.
c to
reflect
the values that were considered
only the dissolved fraction
of metals is toxic to aquatic life, Illinois EPA proposed
Id. During the January 29, 2002
91
d ischargers
that
would
have problems com
(which included new water quality standards for nic
the Matter
302.105, 302.208(e)-(2),
,302.504(a),
302.575(
04.120
Second, the District
Illinois EPA re
The District
not
aware of any
sed the
dards
. Code
41(h), and Proposed 35 Ill. Adm.
02-11 at 99-100 (January 29,
tings and numerous discussions
33
I llinois EPA on
October 30,
2007,
to
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
a
situation regar
ickel
and zinc
During that
meeting,
Illinois EPA advised the District that
a
request
to extend the compliance
schedule in the permit
was premature, but could be considered at
a later date.
the District and AD
llinois
dition,
on December
4, 2008. During that meeting,
Illinois EPA also recommended
that the District submit an application to modify its
o extend the compliance schedule contained
therein.
modification request application to
inois
EPA on January 12, 2009, a copy of which is attached hereto
as Exhibit 1. The
ed supplemental information
to Illinois EPA on April 3, 2009. See
Exhibit
J. On May S, 2009, Illinois EPA posted for public notice
on
its website
a draft
posed
for nickel and zinc from two years to three years.
As of the date of the
issued by Illinois EPA. While the Distri
ified
it
has not been
fficient time for a ruling on this request
for variance.
ween Illinois EPA, the District
nce w
according to the schedule also contained in
the p
ible while continuing
to operate both facilities until ADM discovered, in mid-
2008, that incoming grain was responsible for significant amounts of nickel in the
effluent sent to t
Upon
this
discovery, the
District
and ADM provided Illinois
34
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
ilable
data and a summary of the issue
as part of the District's Third Interim
Report.
See Exhibit F. In light of this information,
Illinois EPA, the District
and ADM
agreed that se
riance
would also be appropriate in
this situation. Because of the
complexity of
the issues at hand, it has taken time
for the D
coordi
with Illinois EPA and to prepare
this Petition. On April 28, 2008,
the District provided a
draft of this Petit
Illinois EPA for its review.
4n May 14, 2009, the District, AD
and
Illinois EPA met to discuss the same.
Further, the District
and
ve spe
to determine the source of the nickel
and zinc discharges, and
estigating methods to decrease
and/or treat those discharge amounts.
The Distr
arts, but they need more
time than is provided by the
the
current NPDES permit (and even more than
the
time.
The cost to
the Distric
s, thus creating an unreasonable
har
100
cubic feet of wastewater discharged, applicabl
1,
commercial and industrial users. The estimated
capital cost alone of
$100,000,000 for reverse osmosis
treatment at the District would result in an additional
et or a 69
operating costs or brine disposal.
The cost to ADM
of the District
hardship on ADM. Whi
in the proposed
modified NPDES permit). Therefore,
the Distri
increase in user charge
without considering
of time and
to comply also imposes
an unreasonable
ues to evaluate
a combination of treatment
35
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
schemes (including
rerouting a steam condensate,
ion exchange, evaporation
and sale as
izer, ultra-filter/reverse
osmosis and
of filtered
material to landfill),
not
yet been able to identify a treatment
plan that is both technically feasible
and
economically reasonable. In
any case, however, design, p
d
start-up would take a minimum of two years
and would entail very large
operating costs. Again, ADM
also cannot cease operations
at its Decatur
Complex without serious
disruption of the local economy.
When discussing arbitrary or unreason
cases, the Boar
Board to dete
cliate compliance
lied
upon the following caselaw:
(415
ILLS 5/35(a)) (11
r egulations designe
any variance is to
be gra
135
111. App. 3d 343,481 N
ions water
variance
petitioner has presented adequate
proo
petitioner to show that
its claimed
nterest in attaining compliance with
owbrook Motel v. IPCB,
a showing can the claimed
hardship rise to the le
unreasonable hardship.
and"s regulations and compliance is
ritual
individual polluter. (Monsanto
Co. v. IPCB, 67
Accordingly, except
is required, as a condition
to
o a plan which is reasonably calculated to
e.
Station v.
. 97-131
at 4-5 (As Corrected June 23, 1997); see also
City of Moline v.
9 (December 19,
1996).
36
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
Therefore, as
set forth above, requiring the District
to
1
S
p ermit effluent limits
for nickel and zinc, which
are based upon the general
use water
ndards formulae provided
for in Section 302.208(e), according
to the
compliance schedule
contained in the current NPDES
permit (or in the proposed
modified NPDES permit), would impose
an arbitrary and unreasonable
hardship on the
on A
for the discuss
VI. COME
potentially on the local economy.
Please see Section V11 below
on regarding the environmental
impact of the variance sought
herein.
LIANCE
PLAN AND SUGGESTED
CONDITIONS
using the following plan
to achieve compliance with nickel
and zinc permit limits by the
end of the requested five-year variance
term, and suggests
111. Admin. Code §
111. Admin.
Code § 304.105 as those sections
1, 2014.
tinue plant
for nickel and zinc, along
with
monitoring
upstream and
downstream of the discharge in the Sangamon
River. Cu
ing for nickel and zinc are performed
twice monthly.
Downstream monitoring has
recently been modified to include four
2007. The Distric
the current
ation
tly acquired an
ing expanded
37
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
4.
Industrial monitoring for nickel
and zinc, currently performed
rly at ADM
and Tate & Lyle and semi-annually
at other
ial users that could
discharge nickel and zinc, has
been
increased
to twice monthly at ADM
and Tate & Lyle.
The District will continue
refinement of pretreatment local
limits
for nickel and zinc necessary
to meet its permit limits, and
will
continue work with ADM and Tate
& Lyle on options for
achieving
compliance with local limits. Ongoing verification
monitoring will be
conducted to confirm that cooling tower
treatment program
ill be undertaking several parallel paths to review
The
District will remain
regarding their
ongoing wo
vings could be
control options and will continue
to meet with ADM
least semiannually and exchange information,
and meet more
frequently as needed.
ill explore the possible
development of stream flow-
based compliance options. As noted above, the District's
discharge does not result
in exceedences of the water quality
standard except very low flow
conditions in the Sangamon River.
A flow-based permit limit would not avoid
the capital cost of
tailed for nickel
treatment, for example, but
flows.
The District will conti
information and bossi
my operated when
,essary zinc reductions.
act
with ADM personnel
ith identifying nickel sources
and
has done some
ible options including
a Water Effect Ratio
calculation and application of a Biotic Ligand
Model. Exploration
of other possibilities such as a site-specific water quality standard
will continue.
Over the course of the first two years
of
the
variance, the District
additional technologies and
compliance strategies. The
gies ultimately used for compliance
may be closely tied to
the compliance strategy to ensure the most practical solution is
d. That is,
technologies will be evaluated based on
rategies involving
both individual process streams
flows. Thus, even if the treatment
of an
ars economically reasonable, if it will not be
to achieve
overall compliance, expenditures on such
38
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
treatment could be
wasted if ADM were required to provide
treatment of the effluent flows.
Thus, neither the District nor
ADM will be in a position to properly evaluate
the cost-
ness
of an overall compliance strategy
have
been evaluated individually.
The following
schedule is a general guide to the key tasks
that
must be completed to determine
the compliance strategy to be
Board should note
that the technologi
forth
below for evaluation are all of the technologies
of which the
ntly aware. Both the District and
will continue to explore
the potential for other technologies and
developments in technologies already evaluated
throughout the
first three
years o -
costs, reliability, and pilot testing as
ADM
will complete technical and economic
feasibility reviews for
the following control
technologies. The reviews will include
determination of technical feasibility, capital and
itation process.
duimmine feasibility and
cunfma i:ý:sults.
chemical company
prietary Precipitation Proces
1- Chemical Precipitation Process
Carbamates or
Organic Sulfides -
begun evaluation of these chemic
provided by GE Betz Company.
further evaluate. Concurrently,
confidentiality agreements and contracts to
low concentration precipitation
Work is underway to complete
experts for
metals
have identified chemi
Exchange Resin -
s of
resins
from the
itable
2009-2010
39
from a quality perspective. Initial tests
indicated
there is suitable capacity to
provide effective nickel reductions.
The
difference between use of spent ion
exchange resin and the ion exchange process
ined to be infeasible is
that the spent resin would not
be
regenerated
which saves significant chemical and energy
costs.
1 and Zinc SQybean Process Stream
for sale of this product as
isms. The purpose
additive. Installation is dependent on
funding
and procurement of customers.
Zinc - BioProducts Process
Stream
Alternative
- ADM is revi
equipment
to thicken a
for use as
and operating
costs are prohibitive
iosis
-
ADM
a
i()n
o
osmosis. Review has
concluded that the technology will work to
reduce both nickel and zinc. However,
he volume of wastewater to be
treated. Continued evaluation of this option
will occur in
combination with other
1
options,
led
concerning a device which breaks
Discussions are
haracteristics of the
its carryover and thus
40
el an
to the District.
1
contacted by
a company which has
the
potential to purchase
all of ADM's sludge.
Testing
of the sludge is scheduled
at the
company's
site. This would
bring AD
into zinc compliance
and close the gap
on
nickel
compliance.
ii.
The
District will complete
the following tasks
on a
parallel
track to ADM's technology
reviews. The
outcome of these
tasks may impact the
feas
the various options
being considered and will
be
valuable in reviewing the
ultimate feasibility of
various control
combinations.
dischargers
eatment limi
discharge
numbers, and
inc - Sludge -
ADM has been
luble/insoluble
ratio of
SlU
how much
of the
the pretreatment limits
should be expressed
as total or soluble limits.
1 strategies based
on one or
more of the feasible
technologies. Develop flow
1 options, pros and cons,
and operating costs.
division managers.
41
10.
The District proposes the following time schedule for achieving
compliance
with
permit limits for
nickel
and
zinc:
January
1,
2010
Submit an interim report to Illinois
EPA describing
progress on eacl
the elements
of
the
compliance plan
above.
July 1, 2010
Submit interim
report,
as
above.
nterim report, as
above.
January 1, 2011
rt, as above.
January
1, 2012
im
report, as above.
Submit a final compliance plan to
Illinois
EPA containing nickel and
ontrols, treatment technologies,
proposed
site-specific water
qua
standards that will achieve
compliance with permit limits.
proposed pe
January
1, 2013
-
Submit interim report, as above.
July 1, 2013
January
1, 2014
July 1, 2014
merim report, as above.
Achieve compliance with nickel
it limits.
g the requested variance would not change any existing environmental or
pact of the District's discharge to the Sangamon River as it has existed
The
District
is not requesting that it be allowed to increa
of nickel and zinc into the Sangamon River.
Instead,
the
District
is as
42
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
allowed
to continue its existing
discharges of these parameters
while it investigates
and
identifies compliance
options.
The
overall
researchers from
of the discharge
on water quality
has been studied
by
ern Illinois University from 1998
to the present. These
biological
slightly improved
water quality
conditions downstream
of
as compared
to upstream, based
on calculations
of the
studies continue
to docum
the District's discharge poin
Macroinvertebrate
Biotic
i
D istrict discharges
Integrity.
The segment of
for pollutants
other than
nickel and zinc; however,
based on the fish community
metrics, there
Fischer and C. Pede
angamon
River segment in the last
20 years. See R.
ois University, Biotic
Assessment of Water Quality
Receiving
Effluent from the
Sanitary District of
attached hereto
a
o R.
Fischer and C. Pede
( July 2008) ,
11 and upstream flows. In the absence
of very dry weather,
the
water quality
standard is regularly achieved
as demonstrated by downstrea
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
environmental impact in recent
water variance
cases, the Board
has relied upon
the following caselaw:
ding to grant
or deny a variance petition,
the Board is required
to balance the petitioner's
hardship in complying with Board
regulations
against
the impact that the requested
variance will have on
the
environment.
See Monsanto Co. v. PCB,
67111. 2d 276, 292, 367
N.E.2d
684, 691 (1977).
Petitioner must establish that
the hardship it would face
from denial of its variance request
would outweigh any
injury to the public
or the environment
from granting the relief,
and "[o]nly if the hardship
outweighs the injury
does the evidence rise to
the level of an arbitrary
or
unreasonable hardship."
Marathon Oil Co. v. EPA, 242111.
App. 3d 200,
206, 610 N.E.
2d 789, 793 (5th Dist. 1993).
See Citgo Petroleum Corporation
and PDV Midwest Refin
CB
2008); see also,
Therefore, as set forth
above, gra
ct of the D strict'
the
July 1, 2014. The District,
however, does not expect
the Board to make its decision in
this matter before the
herefore, the District is see
retroactive variance.
However, if Illinois EPA issues
the modified
rmit
with
the extended compliance date, the District
will seek a variance that will,
begin on July 1,
2010, and end on July 1, 2014.
If that is the case, the District
would not need the
variance
to apply retroactively.
. Illinois EPA,
io
pril
21, 2005).
of
change
44
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
The Board has previously considered numerous
requests for retroactive va
and has stated
the
following
w
11 not apply retroactive starting dates for variances
where the
. . The Board has also provided retroactive
procedural delay that was not the petitioner's fault or was the
fusion over federal
regulations....
Another reason for not applying a retroactive
starting date is if the
petitioner's hardship is self-imposed as a result of the
petitioner's
inactivity or faulty decision-making.... The Board may grant a
retroactive
variance if the petitioner has diligently sought relief and has
made a good faith
effort
toward
achieving compliance with Board
tioner has filed late and the delay was the petitioner's fault....
of Canton v. Illinois EPA, PCB 02-42 (April 4, 2002). (Citations omitted.)
In this
ict a
l ance
jet's
faulty decision-making. In fact, since
even
it,
the
Distric
ith the nickel and zinc effluent li
arch of 2007, and continued through November 2007. The District
discovered, however, that the nickel and zinc limit issues were much more complex than
gnificant amounts of time and resources
ing to determine the source of the nickel and zinc discharges, and investiga
methods to decrease those discharge amounts. Th
more
fully evaluate the issues and find
adequate
solutions.
Finally,
the District
has had
several meetings and
numerous
discussions with
ois EPA regarding the best means to address the situation regarding the District's
45
nickel and zinc
limits. The District met with Illinois EPA
on October 30, 2007, to
apprise
Illinois EPA. of the situation regarding
the nickel and zinc limits. During that
meeting, Illinois EPA advised
the District that a request to extend the pe
schedule was
pre
ompliance
be considered at a later
date. In addition, the District
met with Illinois EPA on December
4, 2008. During that meeting, Illinois
so
recommended
that the District submit an application
to m
d the compliance schedule
contained therein. The District submitted its
permit modification
request application to Illinois EPA on
January 12, 2009.
so submitted supplemental information
to Illinois EPA on
years to three
years. As of the date
roposed to extend the schedule
of compliance for nickel and zinc from two
odified NPDES permit for
the
District.
See Exhibit
, 2009, Illinois EPA posted for public notice
on
this Pet
late 2008, discussions continued between Illinois
best means to address the District's nickel
and zinc issues. The
iance with the nickel limit in the
ossible while continuing
to operate both facilities until
permit, according to the schedule also contained
in the permit, would
2008,
that incoming grain was responsible fo
ficant
amounts o
d, in mid-
District and ADM provided Illinois
ilable
data and a summary of the issue as part of its Thi
ibit F. In light of this information, Illinois
EPA, the District and ADM agreed
46
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
Id
also be appropriate
in this situation. Because of the
complexity
of the issues at hand, it has taken time for the District
and ADM to coordinate
with Illinois
using a significant portion of its resources
on the distribution of the federal stimulus
funds, and as a result, has not been able to commit as many resources
as needed for this
project. On April 28, 2408, the District
provided a draft of this Petition to Illinois EPA
view. On May 14, 2009, the District, ADM and Illinois EPA
met to discuss the
same.
should grant the District a partially retroactive variance in
this matter.
ix.
d to prepare this Petition. In
addition, Illinois EPA has recently been
is resnonsible for
that
immediate
compliance
415
/35(a). The
however, only to the
with applicable federal law. See 415 ILCS 5/
of the Board rules states the following
with regard to
consistency with
ces from the Board's water
(b) All petitions
for variances from Title III of the Act, from 35 Ill.
ubtitle
C, Ch. I "Water Pollution", or fro
pollution related requirements of any other Title of the Act
or
Chapter of the Board's regulations, must indicate whether the
47
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
-d may grant the relic
ant to Section 208 of the
CWA (33 USC 1288).
35 111. Admin. Code § 104.208(b).
The
Board
a number of cases, pursuant
take such action. See e.
L.L.C. v. 111
scent with
the Clean
USEPA effluent guidelines and
lations, or any area-wide waste
treatment management plan approved
by the Administrator of
standards, any other feder
(CWA) (33
iously granted variances from State water
est Refining,
05-85 (April 21, 2005) (which granted
a variance from the
Board's general use
and secondary contact water
solids, 35 111.
i Code §§ 302.208(8) and 302.407); Citgo Petroleum
Corporation
linois v. Illinoi
06-137 (September 7, 2006) (which granted a variance from the Board's
i icral use water quality standard for
dissolved oxygen,
ation,
the instant vari
law.
Pursuant to 35 111. Adm
X1.
ition.
of this Pet
ct waives its right to a
ict and ADM are filing affidav
ltaneously
herewith.
Please see the
Affidavit
of
Timothy
48
ids in
authority and discretion,
consistent with federal law, to
no app
§ 302.206).
that preclude
iance is consistent wi
which is filed on
behalf of the District,
and the Affidavit of Mahlon Kaloupek,
which is filed on behalf of
X1T.
CONCLUSION
This Petition satisfies the requirements
of
Part
104 of the Board rules, in
describes the regulations from which the
variance is sought; descri
nature
of the
s activity that is the subject of the proposed variance;
describes why compliance
with the regulations cannot be achieved by the
compliance date; describes the efforts that
would
be
necessary
for the District to a
mediate compliance
with the
ibes why immediate compliance with
the regulation would impose an
arbitrary or unreasonable
hards
describes the condit
includes a detailed description of a compliance plan;
oses a beginning and ending date for
law; includes affidavits
veri
In
summary, the District i
allow it more time to continue its eva
ion
of adequate
solutions
regarding
its nickel and zinc discharges. The District's variance request stems
ickel and zinc water quality standards,
anticipated to adversely impact
any Illinois dischargers.
However, when the Distric
effluent limi s for nickel an
of the da
ermit was renewed, Illinois EPA imposed
new
et the more stringent
standards.
ains the water within Lake Decatur for
the City
a hearing in this matter,
ing the Board to grant it a five-year variance to
of Decatur's water supply, during dry weather, there
are times when there may be no
49
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
discharge
downstream to the Sangamon River into
which the District discharges. As
a
result, the District could not be granted
a mixing zone, and the District's
effluent limits
directly reflect the
water qu
Even so, given that the only intentional
uses of nickel and zinc at ADM, one
of
most significant industrial users (and a significant
contributor to nickel and
zinc loading),
were as zinc-containing cooling
tower treatment chemicals and nickel
catalysts, the D trict
and AD
substitutes
for those chemicals. 0
while ADM's
use of zinc has been eliminated,
ADM has been unable to find a substitute for
kel catalyst, and it has had limite
through operational and housekeeping
measures.
More importantly, howeve
ially believed that the limits could be met
by
finding
come into
its Decatur Complex
through the corn and soybeans it processes, such that the
presence
zinc is not limited to a few wastewater streams, thereby
greatly increasing
and zinc in its discharge and to investigate compliance
options, the District could
not de
onstruct and commence operation of any adequate
liance
schedule set forth in its NPDES
1
lso could not design, permit,
operation of any adequate treatment
system in accordance with
the compliance schedule.
r ,
a nd the existing aquatic life will not be adversely
impacted
through the granting of this variance since the amount
of nickel and zinc to be discharged
50
would not increase
beyond historical levels.
This variance is necessary
for the District to
continue its evaluation
and investigation of compliance
options.
tioner, the Sanitary
District of Decatur, respectfully
requests
that the
Board grant a variance from the
water quality standards for
nickel and zinc, as set
forth in Section 302.208(e),
and from the
through
Section 304.105. In additio
ould otherwise
be imposed
t of Decatur
respectfully
requests the Board to order
the Illinois EPA, pursuant
to Section 309.184, to modify the
ecatur's NPDES cons
Petition.
stmt
with the variance requested
in this
By:
_/s/Katherine
D. I-Iodge
One of Its Attorneys
C . I1url;ins
3150 Roland
A%
Id,
Post Office Box 57'76
IT R
s 1D0D:001[Fil/Petition for Variance-
nickel and z
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
BEFORE THE ILLINOIS POLLUTION
CONTROL BOARD
SANH ARY DISTRICT OF
)
Df-CATLR,
)
Petitioner,
)
v.
)
PC13
_
_
1
(Variance
-- Water)
If
H
N OI
S FNVIRONMENTAL
PRur rCTIO N AGENCY.
Respondent.
}
AFFIDAVIT OF MAHLON
1KALOUPEK
I. Mahlon
Kaloupek, being first duly sworn on
oath, depose and state
as
follows:
I .
I
am currently employed as the Plant Advisor
at Archer Daniels Midland
Company ("ADM") in Decatur. Illinois.
a position which I have held
since !Flay 2001.
Prior to my employment
as Plant Advisor, I held the follow ing
positions at ADM:
Production Support
Chemist from July 1974 to July 1475:
Assistant Quality
Control
I.aboratory
Manager from July 1975 to
March 1977: and Plant Technical
Superintendent
from 'March 19%7 tea play 2001.
1 receivLA a Bachelor
of Science in Chemistry
from Coe
College in Cedar Rapids.
Iowa.
I
p
articipated i
n the preparation o f
t
he Petition
fir V ariance
dated
June 15.
2 009, to the extent
it discusses A DNI.
3 .
1 have read the
Petition fir Variance
dated June 15, 2009,
and based upon
my
personal
knowledge
and belief. the
facts stated therein with regard
to ADM are
true
and correct.
FURTHER
AFFIANI
SAYETH RIOT.
1111\
Subscribed and sworn
to before tic
this
,`
day
of Jyne. 2009.,
I
'it)()!? F)(!1 1 di :flid,ttH
orMahlon Keroupek
+ ++++"
....
a "t ++++++++*+
+ "OFFICIAL SEAL" +
Mahlon Kaloupek
+
DAWN M L AZELL-J
ACKSON
+
+
NOTARY
PUBLIC,
STATE
OF ILLINOIS +
+ MY cobvissic; EXPIRES 08.22.2010
+
+ t+ý+++.
,.* t4+*+.*"+++
BEFORE THE ILLINOIS POLLUTION CONTROL
BOARD
SANITA
OF
DECATUR,
)
)
Petitioner,
)
P
CB
(Variance - Water)
OIS ENVIRONMENTAL
PROTECTION AGENCY,
Respondent.
)
MOTHY R. KLUGE
1, Timothy R. Kluge, being first duly sworn on oath, depose and state as follows:
1 .
I am currently emp
o f Decatur ("District") in Dec
Prior to July 2007,1 was employed by the Illino
tary Distric
July
2007.
ental Protection Agency for
ars, where I held various positions, including Field Opera
trial Permit Unit Manager and field engineer, all within the
S cience in Chemical
n-Urbana and a Masters of Science
I participated in
the
pre
it discusses the D
3.
1 have read the Petit
I llinois University at
my personal knowledge and belief, the facts stated therein with regard to the District are
true and correct.
Subscribed and sworn to before me
+++++++++++++++++++....
this 15th day of June, 2009.
+
"OFFICIAL
SEAL"
+
+
MARLA
K DURST
+++++++i
+
+
MY
NOTARY
COMMISSION
Puguc,
++
++++
EXPIRES
STATE
++++++++f.
OF
4713.2411
auNOls
+
+
+
SL)0D:001/Fil/Affidavit of Tim Kluge
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *
I, Katherin
attached ENTRY
SCE OF LAUREN C. LURKINS, PETIT
TE OF SERVICE
Hodge, the undersigned, hereby
certify that I have served the
attached exhibits, AFFIDAVIT
OF
MAHLON
Assistant
Clerk of the Board
ois Pollution Control Board
Chicago, Illinois
0
reet,
Suite 11-500
ail on June 15, 2009; and upon:
ronmental Protection Agency
J 1'R V (1F
LOUPEK and AFFIDAVIT
OF
S DCJD:001/Fil/N0F-C0S - Petiti
Electronic Filing - Received, Clerk's Office, June 15, 2009
* * * * * PCB 2009-125 * * * * *