ILLINOIS POLLUTION CONTROL BOARD
    July 7,
    1995
    IN THE MATTER OF:
    )
    PETITION OF CONVERSION
    )
    AS 93-5
    SYSTEMS,
    INC. FOR ADJUSTED
    )
    (Adjusted Standard-Land)
    STANDARD FROM 35 ILL.
    ADM.
    )
    CODE PART 811
    (Monofill)
    )
    OPINION
    AND
    ORDER OF THE BOARD
    (by C.A. Manning):
    This matter is before the Board on a petition for an
    adjusted standard filed by Conversion Systems,
    Inc.
    (CSI)
    on July
    2,
    1993.
    CSI seeks adjusted standards from the requirements of
    35
    Ill.
    Adin.
    Code Part 811,
    standards for new solid waste
    landfills, Sections 811.105, 811.306—309,
    811.313,
    811.314,
    and
    811.321,
    as they apply to its Poz—O-Tec®
    (Poz—O—Tec)
    materials.
    These materials are produced through a patented stabilization
    process utilizing flue gas desulfurization
    (FGD)
    sludges and ash
    produced by coal—burning power generation facilities.
    CSI seeks
    the adjusted standard in order to allow Poz—O—Tec materials to be
    disposed of in a inonofill without the need for a liner, cap or
    leachate collection system.
    Based upon the record before it and upon review of the
    factors involved in the consideration of adjusted standards, the
    Board finds that petitioners have demonstrated that grant of an
    adjusted standard is warranted.
    Accordingly, for reasons more
    fully set forth below, the Board hereby grants CSI an adjusted
    standard from Sections 811.105,
    811.306—309,
    811.313,
    811.314,
    and 811.321.
    PROCEDURAL HISTORY
    CSI originally filed
    a petition for adjusted standard,
    docketed as AS 92-9, concerning its Poz-O-Tec materials on August
    24,
    1992.
    That petition was dismissed by the Board on March 25,
    1993, pursuant to CSI’s request to voluntarily withdraw the
    petition.
    The petition before the Board in the present
    proceeding was filed on July
    2,
    1993.
    Concurrently with the
    filing of this petition, CSI filed a separate petition for
    adjusted standard, docketed as AS 93-4, wherein CSI seeks relief
    from the requirements of
    35 Ill. Adm.
    Code Part
    811 so as to
    allow owners or chemical waste landfills accepting only
    FGD
    sludges and coal combustion wastes to use Poz—O—Tec as a liner
    and cap material.
    Also on July 2,
    1993,
    CSI filed a “Motion Regarding
    Procedural Matters,3’ wherein CSI requested that it be allowed to
    incorporate by reference the entire record from AS 92—9.
    CSI
    also requested that the Board rule upon the
    issue of whether its

    2
    failure to include site—specific information would make adjusted
    standard relief unavailable.
    On July 20,
    1993,
    the Illinois
    Environmental Protection Agency
    (Agency)
    filed a response to this
    motion and
    a motion to dismiss, which argued that the Adjusted
    Standard process was an inappropriate vehicle for the relief
    requested by CSI.
    CSI filed a reply to the Agency’s response.
    The Board issued an order on July 22, 1993, which granted CSI’s
    motion to incorporate the record in AS 92—9.
    On August 26,
    1993,
    the Board issued an order, with two Board Members dissenting,
    which allowed CSI’s petition to proceed as an adjusted standard.
    (See Board Order of August 26,
    1993,
    B. Forcade and CA.
    Manning
    dissenting.)
    In its August 26,
    1993
    order,
    the Board expressed
    no opinion as to
    the merits of the petition.
    The Agency filed two motions for extensions of time to file
    its response in order to allow the Agency to substitute counsel,
    and in order to allow negotiations between the parties.
    The
    Board granted both extensions of time,
    the second of which
    granted the Agency an extension until May 23,
    1994 to file its
    response.
    The Board received CSI’s Certificates
    of Publication on
    August 2,
    1993, which indicated that notice of the proposed
    adjusted standard was published
    in the State
    Journal-Register
    on
    July
    5,
    1993,
    and in the Chicago
    Sun-Times
    on July
    3,
    1993.
    No
    requests for public hearing were received,
    and no hearing was
    held
    in this matter.
    However,
    on May 19, 1994,
    the Board
    assigned a hearing officer to this matter, and directed the
    parties to hold a pre-hearing conference, which was held June 22,
    1994.
    Subsequently, because
    the parties wished to continue
    negotiating, the hearing officer issued an order directing the
    parties to file status reports on or before November
    1,
    1994.
    The Agency filed its response to the petition for adjusted
    standard on November 3,
    1994,
    recommending that the adjusted
    standard be granted, subject to certain additions and amendments.
    On November 14,
    1994 CSI filed a motion for leave to file a reply
    to the Agency response which the Board granted.
    The reply
    indicates that CSI is in agreement with the Agency’s proposed
    amendments to the adjusted standard.
    On May 5,
    1995, CSI filed a motion requesting that the Board
    follow its August 26, 1993 order.
    The Board finds the motion
    moot for the reasons set forth below in the opinion.
    THE ADJUSTED STANDARD PROCESS
    -
    SECTION
    28.1
    OP THE ACT
    ThG Board’s rosponsibility
    in this inattsr arisas
    from tha
    Environmental Protection Act
    (Act)
    (415 ILCS
    5/1 et seq.).
    The
    Board is charged therein to “determine, define and implement the
    environmental control standards applicable in the State of
    Illinois”
    (Section 5(b)
    of the Act)
    and to “grant
    .
    .
    .
    an

    3
    adjusted standard for persons who can justify such an adjustment”
    (Section 28.1(a)
    of the Act).
    More generally, the Board’s
    responsibility in this matter is based on the system of checks
    and balances integral to Illinois environmental governance:
    the
    Board is charged with the rulemaking and principal adjudicatory
    functions,
    and the Agency is responsible for carrying out the
    principal administrative and enforcement duties.
    Section 28.1 of the Act provides that a petitioner may
    request, and the Board may
    adopt an individual adjusted standard
    different from the standard that would otherwise apply to
    petitioner pursuant to a rule of general applicability.
    Such a
    standard is called an adjusted standard.
    The general procedures
    that govern an adjusted standard proceeding are found at Section
    28.1 of the Act and within the Board’s procedural rules at 35
    Ill. Adm. Code Part 106.
    Where, as here, the
    regulation of general applicability does
    not specify
    a level of justification required for a petitioner to
    qualify for an adjusted standard,
    the Act at Section 28.1(c)
    specifies four demonstrations that must be made by a successful
    petitioner:
    1)
    Factors relating to that petitioner are substantially
    and significantly different from the factors relied
    upon by the Board in adopting the general regulation
    applicable to that petitioner;
    2)
    The existence of those factors justifies an adjusted
    standard;
    3)
    The
    requested standard will not result in environmental
    or health effects substantially and significantly more
    adverse than the effects considered by the Board in
    adopting the rule of general applicability;
    and
    4)
    The adjusted standard is consistent with any applicable
    federal
    law.
    Instead of seeking relief that is specific to an individual,
    or a site, CSI is requesting that an adjusted standard be granted
    from certain sections of Part 811,
    so that those facilities which
    produce FGD sludges and ash (approximately 45 coal burning power
    generation facilities), may purchase CSI’s Poz—O—Tec process and
    dispose of Poz—O-Tec material without having to comply with the
    existing Part 811 liner and leachate requirements.
    As statad praviously the Board denied an Agency motion to
    dismiss the instant petition and that of AS 93-4.
    Since that
    time, the Agency and CSI have come to agreement as to the
    requirements that would be imposed on the purchasers
    of the Poz-
    O—Tec process, and the Agency has filed a recommendation to that

    4
    effect with the Board.
    However,
    in reviewing the language of the proposed adjusted
    standard, the Board finds that it imposes requirements on the
    purchasers and
    users
    of the Poz—O—Pec process,
    and not strictly
    upon CSI, the individual company who sought and to whom we grant
    this adjustment to the rules of general applicability. Therefore,
    in order to ensure that the users of the Poz-0—Tec materials for
    which the adjusted standard is granted, clearly understand and
    are legally and regulatorily committed to proper use of the Poz-
    O—Tec process product, the Board will also open a rulemaking
    docket to consider incorporating this adjusted standard into a
    rule of general applicability governing the Poz-O-Tec process of
    CSI, pursuant to Sections 27 and 28 of the Act.
    The Board intends to use this docket to adopt the language
    of the adjusted standard, as agreed to and drafted by CSI and the
    Aqency, as a new Part 816,
    entitled “New Utility Waste
    Landfills.”
    Additionally, we will propose amendments to Part
    807,
    810,
    and 811 in order to provide for consistency with a
    proposed, new Part 816.
    We also believe that it is appropriate
    for the Board,
    and we note that
    it
    is within our discretion,
    to
    consider a rule of general applicability for the Poz-O-Tec
    materials pursuant to Section 27 and 28 of the Act.
    The following is the Board’s examination of the technical
    merits of the adjusted standard.
    APPLICABLE REGULATIONS PROM WHICH CSI
    SEERS AN ADJUSTED STANDARD
    CSI seeks an adjusted standard from the requirements of 35
    Ill. Adm.
    Code Sections 811.105,
    811.306—309,
    811.313,
    811.314,
    and 811.321.
    These rules are contained in Subpart C of Part 811
    of the Board’s landfill rules.
    Part 811 prescribes the standards
    applicable to new solid waste landfills, and Subpart C of Part
    811 prescribes those standards specifically applicable to
    chemical and putrescible waste (chemical waste)
    landfills.
    Section 811.105 sets forth the compaction requirements.
    811.306
    prescribes the liner requirement.
    811.307-309 prescribes the
    standards and protocol for leachate.
    811.313 and 811.314 set
    forth intermediate and final cover requirements.
    Each of these
    is discussed in greater detail below.
    Section 811.105 provides, among other requirements, that
    wastes shall be deposited at the lowest part of the active face
    and compacted to the highest achievable density.
    Among the requirements of Section 811.306, this section sets
    forward the regulatory requirements for liner systems including
    that units shall be equipped with a leachate drainage and
    collection system and compacted with an earth liner.
    The earth

    5
    liner standards are to have a minimum allowable thickness of 1.52
    meters (or five feet)
    and that it shall be compacted to have a
    maximum hydraulic conductivity of 1x107 centimeters per second.
    Sections 811.307 through 811.309 provide the requirements
    for the leachate drainage,
    collection and treatment and disposal
    systems.
    These requirements provide for drainage layers
    overlaying
    a liner system. They set forth the drainage layer
    thickness. The rules provide for the design of the collection
    pipes of the leachate collection system, how the system shall be
    constructed and of what material.
    Section 811.309 provides for
    leachate storage and treatment standards for on—site treatment,
    disposal, for the facilities’ tank,
    pond,
    lagoon and basin
    design,
    recycling, monitoring, discharge to off-site treatment
    works,
    and leachate management systems.
    Sections 811.313 and 811.314 set forth the requirements for
    intermediate and final cover.
    The intermediate cover rules
    consists of grade and thickness requirements. The final cover
    rules contain standards for thickness,
    area to be covered,
    permeability, compaction standards, material requirements and
    timing for placement.
    Section 811.321 contains the waste placement rules at a
    landfill requiring that waste be placed at the lowest portion of
    the landfill and shall be moved to the highest portion.
    The rule
    also allows for placing the waste in other areas depending the
    existence of certain conditions such as climate,
    topography and
    the placement of groundwater monitoring wells.
    PROPOSED ADJUSTED STANDARD
    In this petition, CSI seeks an adjusted standard to allow
    Poz-O—Tec materials to be disposed of in a inonofill without the
    need for a liner, cap or leachate collection system. Poz—O—Tec
    materials are produced through a patented stabilization process
    which uses forced—oxidized flue-gas desulfurization scrubber
    sludge and coal combustion ash as raw materials.
    (Pet. at 1.)
    The scrubber sludge is directed to a scrubber blowdown tank,
    and
    then to primary and secondary dewatering systems.
    (Pet.
    at
    7.)
    The dewatered sludge is then directed to a mixer where fly ash
    and lime are added.
    The materials are mixed and then stabilized,
    producing a highly impermeable monolithic mass
    (Pet.
    at 7), with
    a high unconfined compressive strength and load—bearing capacity,
    and the capability for autogenous healing of small cracks and
    fissures
    (Pet. at 2-3).
    The material continues to cure over a
    periodof years, becoming stronger.
    The Poz—O-Tec materials meet
    the classification criteria for
    inert waste, with the exception
    of concentration of total dissolved solids
    (TDS)
    and sulfates in
    the leachate produced.
    (Pet.
    at 2.)

    6
    Poz—O—Tec materials have been used since 1977
    as bases for
    highways, parking lots and airport runways.
    (Pet.
    at 3.)
    They
    have been used to construct aquaculture ponds, artificial ocean
    reefs, and have been formed into construction blocks and used as
    a substitute for aggregate or stone for the production of
    concrete blocks.
    (Pet.
    at
    3)
    They have also been used to
    prevent erosion along coastlines and railway embankments,
    as a
    monolithic fill material, and to reclaim strip mines from coal
    mining.
    (Pet.
    at
    3.)
    CSI is seeking this adjusted standard in order to market the
    Poz—O—Tec process to approximately 45 coal combustion power
    generation facilities in Illinois. There presently no such
    purchasers in Illinois
    (Pet. at 4); however, this may be because
    such use may not be permitted pursuant to current Board
    regulations, and due to the cost differential between surface
    impounding and landfilling FGD waste subjected to the Poz-O—Tec
    process pursuant to the chemical waste landfill rules.
    C5I
    believes this is because surface impoundments are largely
    unregulated under current law.
    (Pet. at 4.)
    In this petition,
    CSI does not seek an adjusted standard
    applicable to a specific site; rather,
    it seeks to allow an
    adjusted standard applicable to its Poz—O—Tec process wherever
    used throughout the state.
    (Pet.
    at 8.)
    All potential users
    are all coal burning facilities that have either baghouses or
    electrostatic precipitators, and would be required to operate FGD
    systems
    in order to use the Poz-O—Tec process made available by
    this adjusted standard.
    (Pet. at 8.)
    The proposed adjusted
    standard would allow each of the coal burning facilities that
    produce combustion waste and FGD to inonofill Poz—O—Tec material.
    The adjusted standard would~~not affect any of the other
    requirements in the chemical waste landfill rules of Part 811
    other than those rules from which CSI’s Poz—O—Tec process and
    material is receiving an adjusted standard today in AS93-4.
    Pursuant to the relief requested by CSI in the instant
    petition and the related petition of AS 93—4, facilities which
    have decided to utilize the Poz—O—Tec process would have two
    available disposal options: monofilling pursuant to the relief
    requested by CSI herein, or constructing a liner and cap of Poz—
    O—Tec materials, pursuant to the adjusted standard relief we are
    granting in AS93-4.
    A facility’s decision as to which option to
    use would be dependent upon the ratio of flyash and sludge in its
    waste stream.
    CSI asserts that most facilities will be able to
    consistently produce high quality Poz-O-Tec materials with a
    permeability less than or
    equal
    to 1x107 cm/sec.
    (Pet.
    at 11.)
    These
    materials
    could
    be
    disposed
    of
    in
    a
    monof ill
    and
    would
    ultimately result in a large, monolithic block of disposed

    7
    material.’
    According to the petitioner, upon the Poz-O-Tec materials’
    production, the material would be placed into a stockpile where
    it would begin to cure and form into a cementitious material.
    (Pet.
    at
    9.)
    It would then be placed upon or adjacent to Poz-O-
    Tec materials already in the landfill.
    (Pet. at
    10.)
    The
    materials would be spread into lifts, rolled to smooth,
    compacted
    and graded so that rainfall would run off and be collected
    without puddling.
    (Id.)
    The monofill would be designed to allow
    for surface run—off from the monofill toward an open end of the
    fill.
    (Pet.
    at 6.)
    The Poz—O-Tec materials, which under AS 93-
    4,
    are predicted to allow for no leachate permeation would
    substitute as a liner, and therefore no liner or leachate
    collection system is required.
    (Pet. at 6.) CSI also seeks relief
    from the requirement that a soil cover be placed on the landfill
    because one of the benefits of Poz-O-Tec materials is that it
    forms bonds with new material as
    it is added to the landfill, and
    does so without seams.
    (Pet.
    at
    6.) Therefore,
    leachate pathways
    are avoided which would otherwise form between lifts of other
    types
    of materials.
    Placing an intermediate cover over the
    materials would jeopardize the structural integrity of
    the
    monofilled material and create a leachate pathway in itself.
    (Pet.
    at
    6.)
    CSI also requests relief from the requirement that
    there be
    final cover placed on the landfill because the material
    itself will serve as
    a low permeability layer.
    (Pet.
    at 7.)
    JUSTIFICATION IN SUPPORT OP THE ADJUSTED
    STANDARD
    -
    THE SECTION 28.1(c) FACTORS
    In support of its petition for adjusted standard, CSI states
    that the chemical waste landfill rules in Part 811, which are
    general rules covering a wide range of wastes,
    are designed to
    1Some facilities will not generate sufficient fly ash
    to
    conBistently
    produce materials with a permeability less than or equal to lx10~’cm/sec. and
    it is these facilities which would instead be producing a sufficient quantity
    of Poz—O-Tec materials
    to construct a liner and cap meeting the
    lxlO’ cm/sec.
    standard.
    This would be accomplished by storing fly ash until an adequate
    supply is available to produce high quality Poz—O—Tec materials.
    (AS93—4 Pet.
    at 8.)
    The landfill would then be constructed and operated in
    accordance with
    the chemical waste landfill rules.
    The adjusted standard relief in AS93-4
    allows facilities to use a Poz—O—Tec liner which is at least five feet thick,
    which has a permeability of
    lxlO1 cm/sec. or less and an unconfined
    compressive strength
    of 150 psi or greater.
    The permeability and unconfined
    compressive
    strength must be verified through the construction and field
    testing of a test pad.
    The landfill must receive for disposal only FGD
    sludges and coal combustion wastes, and must be constructed at least five feet
    above the water table.
    The cap could be constructed of the same material as
    the liner, and must be
    at least three feet thick.
    Site owners would be
    required to do site-specific contaminant modelling,
    groundwater modelling and
    assessment and remedial action.

    8
    protect the environment regardless of the degree of hazard of the
    wastes.
    CSI points out the adjusted standard it seeks applies
    only to generally inert wastes.
    According to CSI, requiring a
    monofill consisting of Poz-O-Tec materials,
    to comply with the
    liner, cap and leachate collection and treatment requirements
    would impose a unreasonable burden upon coal combustion power
    generation facilities.
    (Pet.
    at 27.) As part of demonstrating
    the unreasonable burden,
    CSI
    has also set forth the compliance
    alternatives available to coal burning power generation
    facilities that produce FGD sludges and ash for disposal.
    Compliance Alternatives
    In its
    original petition
    in AS 92—9, incorporated
    by
    reference into this proceeding, CSI presented an analysis of
    existing management alternatives for FGD by—products currently
    available to coal burning power generation facilities.
    This
    analysis was based on a study performed for CSI by Environmental
    Resources Management
    (ERN).
    ERM
    investigated the following
    management options for disposal of FGD by-products:
    1) Wet Impoundment/Gypsum
    Stacking
    This option consists of
    directing the
    FGD
    slurry from a
    scrubber system to a
    settling pond, where FGD solids are settled out.
    Effluent
    from the settling pond is either recycled into the scrubber
    system or treated and discharged, while settled solids are
    periodically removed.
    The
    settled solids can be stacked
    around the perimeter of the settling pond to increase
    its
    height, or can be stored in a reclaim area for subsequent
    landfill disposal;
    2)
    Macroencapsulation of Dewatered
    FGD Sludge
    This
    option
    consists of dewatering the FGD sludge and placing it into a
    lined landfill.
    The landfill would be capped upon closure.
    The landfill could be used for either disposal of the POD
    sludge, or co—disposal of the FGD sludge and fly ash;
    3) Disposal of Dewatered FGD Sludge in an Unlined Cell
    -
    This option is identical to option #2, Nacroencapsulation of
    Dewatered Sludge, with the exception that the materials are
    disposed of in an unlined cell; and
    4)
    Fixation and Stabilization of FGD Sludge (Poz—O-Tec
    process)
    -
    This option involves treating the FGD sludge with
    the Po~-O—Tecprocess and disposing of
    it in a lined or
    unlined landfill.
    ERM
    investigated
    each of these options using
    a theoretical
    model power plant generating
    600
    NW
    or more of power,
    burning
    3
    sulfur coal with 12
    ash and a heat content of 11,000 Btu/lb, and
    using a 90
    efficiency scrubber.
    Options were investigated under
    scenarios where the disposal site was unlined, singly lined, or

    9
    doubly lined, and where the leachate was trucked or piped, and
    where FGD sludge was disposed of alone or co—disposed with fly
    ash.
    The
    ERN
    study analyzed the costs for each disposal option,
    including total capital cost, total yearly operation and
    maintenance cost,
    and total annualized cost.
    CSI asserts that
    all options using a double liner are economically unreasonable,
    and unlined options do not satisfy regulatory requirements.
    The
    ERM
    study estimated the total annualized cost for each
    option using a singly-lined landfill and piping for leachate as
    follows:
    Disposal Method
    Total Annualized Cost
    Wet Pond/Stacking
    $22.95 million
    Macroencapsulation
    $16.60 million
    (gypsum only)
    (additional cost of $2.8
    million for disposing of fly
    ash)
    Macroencapsulation
    $15.75 million
    (gypsum
    and flyash)
    Poz—O—Tec Process
    $17.16 million
    The
    ERM
    study found that the cost of disposal using the Poz-
    0-Tec process with no liner was $15.87 million.
    CSI asserts that
    disposal using the Poz—O-Tec process and a liner constructed of
    Poz—O—Tec which meets the ixio7 cm/sec standard for permeability
    would be somewhere between the $17.16 million cost when using a
    liner and the $15.87 million cost for unlined disposal.
    The
    Agency is in general agreement with CSI’s discussion of the
    various disposal options,
    although the Agency did not conduct a
    separate investigation of these costs.
    In the instant petition, CSI has addressed the issue of
    compliance alternatives from the perspective of a facility which
    has decided to use the Poz-O-Tec process.
    (Pet. at 13.)
    For
    these facilities,
    CSI states that the only cost differential
    between compliance with the chemical waste landfill rules and the
    monofill relief sought is that a facility benefiting form the
    adjusted standard would not be required to construct a liner,
    a
    cap or a leachate collection system.
    Though CSI also requests
    relief from the compaction,
    intermediate and waste placement
    rules,
    this relief is of a technical nature and has no
    significant impact on costs.
    (Pet. at
    13,
    n.5.)
    Using the
    ERM
    report,
    CSI estimates the savings to be the following:
    Assuming
    that waste disposal needs for 30 years, the capital costs for

    10
    liner construction would be $4,356,250
    (Pet.
    at 14); A cap, which
    would be approximately 60
    of the liner costs because it would be
    three feet thick versus five feet for the liner,
    would then costs
    $2.6 million
    (Pet.
    at 14);
    and,
    a leachate system would cost
    approximately $264,000
    (Pet. at 14—15.)
    CSI thus estimates that
    these facilities could save approximately $7.2 million under the
    adjusted standard versus, the compliance alternative.
    (Pet.
    at
    19.)
    Health and Environmental Effects
    Section 28.1(c) (3)
    According to the petition, allowing for the disposal of Poz-
    0—Tec materials in a inonofill without using
    a liner,
    or a cap
    will provide the following environmental advantages:
    1)
    The Poz—O—Tec process reduces the volume of the total amount
    of material disposed of by at least 40
    through
    densification as compared to surface impounding of the
    unstabilized materials, thereby reducing the disposal area;
    2)
    Due to the greater compressive strength and lesser
    liquefaction qualities of the stabilized material
    as
    compared to the unstabilized material, the Poz—O—Tec
    materials can be stacked higher with steeper slopes than the
    unstabilized material, again reducing the disposal area
    needed;
    3)
    There are some viable markets for the sale of stabilized
    material, thereby reducing the amount of material which must
    be disposed of, and the in—place stabilized material is more
    readily available for beneficial uses should more viable
    markets become available; and
    4)
    It preserves clays which form a natural protective barrier
    for groundwater where it is naturally located from mining
    for use as liner or cap material.
    (Pet.
    at 22—23.)
    Additionally, when Poz-O-Tec materials are disposed of
    in
    monofill material, according
    to
    CSI, they provide environmental
    protection equivalent or superior to earthen or geomembrane
    liners and caps.
    (Pet.
    at 22—23.)
    A landfill using Poz—O—Tec
    materials will generate leachate which
    is similar to that
    produced under any disposal option investigated by
    ERN.
    A
    landfill which uses Poz—O—Tec would generate leachate which meets
    the Board’s Inert waste standards,
    except for total dissolved
    solids
    (TDS)
    and sulfates.
    (Pet.
    at 20)
    However,
    a landfill
    which uses Poz-O-Tec will generate significantly less leachate
    than those using other materials.
    (Pot.
    at 20.)
    While Poz—O-Tec
    materials are less plastic than clay, they are far stronger.
    (Pet. at 22.)
    If any small cracks or fissures were to develop,
    the autogenous healing properties of Poz—O—Tec would heal them.
    (Pet. at 22.)

    11
    Consistency with Federal Law
    CSI states, and the Agency agrees, that none of the
    requirements from which relief is sought were promulgated, in
    whole or in part, pursuant to federal requirements.
    (Pet. at 29.)
    Therefore the requested relief can be granted consistent with
    federal law.
    AGENCY RECOMMENDATION
    In its response to the petition for adjusted standard, the
    Agency generally agrees with the information presented in CSI’s
    petition, and recommends that the adjusted standard be granted.
    The Agency made several recommendations to CSI’s proposed
    adjusted standard language, with which CSI is in agreement.
    The
    recommended language changes are consistent with those adopted by
    the Board today in AS93-4 and are included herein in our order.
    CONCLUSION
    CSI has demonstrated that there are factors relating to the
    disposal of Poz—O—Tec materials in a monofill without the
    use
    of
    a liner,
    cap or leachate collection system which are
    substantially and significantly different from the factors relied
    upon by the Board in adopting the regulation of general
    applicability.
    In this case, these factors justify an adjusted
    standard.
    CSI’s Poz-O-Tec process was not considered by the
    Board when it drafted the landfill rules
    (and as an aside,
    CSI
    did not participate in that rulemaking proceeding).
    Further,
    this adjusted standard may be granted consistent with any
    applicable federal law.
    The Board hereby finds that petitioners have demonstrated
    that an adjusted standard is appropriate in order to allow the
    monofilling of Poz—O-Tec materials pursuant to Part 811, without
    the required use of a liner, cap or leachate collection system.
    Therefore the Board will adopt an adjusted standard for the use
    of CSI’s Poz—O—Tec materials and process subject to the
    conditions agreed upon by the Agency and CSI.
    This opinion constitutes the Board’s conclusions of law and
    findings of fact in this matter.
    ORDER
    The Board grants an adjusted standard,
    pursuant to 415
    ELCS
    5/28.1, to the Poz-O—Tec process and materials of Conversion
    Systems, Inc. subject to the provisions and conditions set forth
    below.
    The Board directs the Clerk or the Board to open a
    rulemaking docket to consider incorporating this adjusted
    standard into a rule of general applicability.

    12
    I.
    Any monof ill consisting solely of flue gas desulfurization
    sludges and coal combustion wastes produced by coal
    combustion power generating facilities utilizing a lime or
    limestone scrubber system shall be exempt from the
    requirements
    of
    35 Iii.
    Adin.
    Code 811.105
    (solely as
    it
    relates to the placement of wastes at the lowest part of the
    active face), 811.306,
    811.307,
    811.308,
    811.309,
    811.313
    (solely as it relates to soil cover),
    811.314(b) (3) (C)
    (solely to the extent that
    it may preclude Poz-O-Tec
    materials from being used as a landfill cap)
    and 811.321
    (relating solely to waste placement), provided that:
    1.
    The materials have been processed using the Poz-O—Tec
    stabilization process from Conversion Systems,
    Inc.;
    2.
    The permeability of the liner material shall be
    demonstrated to be less than or equal to 1x107 cm/sec
    after placement and curinq based upon a qeometric
    average
    of
    those cylinders tested for permeability
    which were formed from a single sample;
    3.
    The material has an uncontined compressive strength of
    greater than or equal to 150 psi using an arithmetic
    average of the strength testing results;
    4.
    The base of the monofill shall be constructed at least
    five feet above the average historical groundwater
    table.
    5.
    A monof ill liner and low permeability cap shall be
    constructed from the Poz-O—Tec materials as described
    in
    the Board’s order in AS 93-4;
    6.
    A drainage layer shall be constructed atop the nionofill
    liner which has a permeability greater than or equal to
    1x10~3cm/sec which extends over the entire liner system
    of the nionofill;
    7.
    The material shall be placed in such a manner that
    it
    will form a monolithic block through placement of the
    material in one to two foot lifts, which are compacted,
    rolled to smooth and graded and sloped such that any
    rainfall rapidly runs off the upper surface without
    puddling;
    8.
    At all times a berm shall be maintained around three
    sides of the landfill mass and the grading shall be
    such that the run-off shall be directed toward the open
    side where it shall be collected for reuse or treated
    (if necessary)
    and discharged pursuant to an NPDES
    permit;

    13
    9.
    The following material testing procedures will be
    implemented:
    A.
    Creation and Sampling of Test Pad
    (1)
    The owner/operator of the disposal site shall
    construct a test pad in accordance with 35 Ill.
    Adm. Code 811.507(a), unless waived by the
    Agency pursuant to subsection
    (b)
    of that section;
    (2)
    The test shall be allowed to cure for 56 days at
    73”Fahrenheit
    (or equivalent cure);
    (3)
    After curing,
    fifty samples will be taken using a
    4 inch diameter coring bit; and
    (4)
    The specimens will be trimmed to proctor cylinder
    size utilizing an abrasive blade masonry saw, and
    tested for unconfined compressive
    strength and coefficient of permeability and
    thirty will be analyzed for their unconfined
    compressive strength.
    B.
    Collection of Production Samples
    Samples will be collected from the production of
    Poz—O-Tec in the following manner:
    (1)
    Utilizing a large scoop, five gallon buckets of
    freshly produced material will be collected at
    uniform intervals during construction of the test
    pad and shipped to a laboratory for analysis.
    (2)
    Five proctor cylinder specimens will be prepared
    from each bucket of freshly produced material.
    Three of these five cylinders will be tested
    for unconfined compressive strength and the other
    two will be tested for permeability.
    (3)
    Additional uncured samples will be taken as
    necessary for preparation and testing to determine
    criteria for moisture content,
    lime content, the
    ratio of fly ash to sludge and in-place density.
    Testing for these parameters shall be conducted in
    accordance with standard test methods appropriate
    for the particular parameter.
    The criteria shall
    be established so as to reasonably ensure that the
    material disposed of will achieve the permeability
    and strength requirements set forth in
    subsection E,
    below.

    14
    C.
    Strength and Permeability Testing
    (1)
    Uncured samples will be taken to a laboratory,
    placed into proctor cylinders,
    compacted to
    simulate field conditions
    (ASTM method D-
    1557-91), cured in sealed containers for 56 days
    at
    730
    Fahrenheit(or equivalent cure)
    and tested
    for coefficient of permeability and unconfined
    strength using the following test methods:
    -
    U.S. Army Corp. of Engineers Engineering
    Manual 1110-2—1906 Appendix VII,
    Falling—Head
    Permeability Test with Permeameter Cylinder.
    -
    ASTM
    Method D5l02; Standard Method for
    Unconfined Compressive Strength of Cohesive
    Soils.
    (2)
    Field samples will be tested using the same
    methods as specified in subsection C(l),
    above.
    0.
    Data Correlation
    Laboratory data and field data will be compared to
    determine any statistically significant differences
    using standard statistical correlation methodologies.
    E.
    Subsequent Testing
    Upon completion of field verification, as described
    above, the owner/operator of the site shall conduct
    QC/QA testing by taking monthly samples of freshly
    produced Poz—O-Tec materials, and sending those samples
    to a laboratory where they will be formed into proctor
    cylinder specimens for testing.
    Two
    of those samples
    will be tested for their coefficient of permeability,
    three for uncorifined compressive strength,
    and one each
    for the parameters set forth in subsection B(3),
    above.
    Laboratory testing for permeability and strength must
    be conducted in accordance with the test methods
    referenced in section C(l)
    of these procedures.
    Test
    results must demonstrate a coefficient of permeability
    of less than or equal to lxlO7 cm/sec using a
    geometric average of the permeability testing results,
    and an unconrinect compressive strength of greater
    than or equal to 150 psi using an arithmetic average of
    the strength testing results.
    10.
    Construction of the full scale inonofill may commence
    immediately upon completion of the test pad.

    15
    11.
    The person or entity using the material in this manner
    shall prepare an acceptable groundwater impact
    assessment pursuant to 35 Ill. Adm. Code 811.371(b),
    812.316, 813.304,
    or 815.203, as appropriate for the
    given facility; and
    12.
    The person or entity using the material in this matter
    shall comply with the Illinois Environmental Protection
    Act (the
    “Act”)
    (415 ILCS 5/1 et seq.) and 35 Ill.
    Adm. Code 811, to the extent those provisions are not
    otherwise addressed herein.
    IT IS SO ORDERED.
    Section 41 of the Environmental Protection Act (415 ILCS
    5/41
    (1992)) provides for the appeal of final Board orders within
    35 days of the date of service of this order.
    The Rules of the
    Supreme Court of Illinois establish filing requirements.
    (See
    also 35 Ill. Adm.
    Code 101.246.
    “Motions for Reconsideration”.)
    J. Theodore Meyer, R.C.
    Flemal and J.Yi concurred.
    I, Dorothy N.
    Gunn,
    Clerk of the Illinois Pollution Control
    Board, hereby certify that the abov
    pinion and order was
    adopted on the
    7tZ
    day of
    _________________,
    1995, by a
    vote of
    7—o
    .
    4.
    /L
    orothy N.
    Gji/rn,
    Clerk
    Illinois Po~7utionControl Board

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