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 * * * * *

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