United States
           Environmental Protection
           Agency
Office of Pesticides
and Toxic Substances
«EPA    Title III Section 313
           Release Reporting
           Guidance
EPA 560/4-88-004J
February 1988
           Estimating Chemical Releases From
           Roller, Knife, and Gravure Coating
           Operations

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            Estimating Chemical Releases From
    Roller, Knife,  and Gravure Coating Operations
    Facilities performing coating operations
 may be required to report annually any
 releases to the environment of certain
 chemicals regulated under Section 313, Title
 III, of the Superfund Amendments and
 Reauthorization Act (SARA) of 1986. If your
 facility is classified under SIC codes 20
 through 39 and has 10 or more full-time
 employees, for calendar year 1987 you must
 report all environmental releases of any
 Section 313-listed chemical or chemical
 category manufactured or processed by your
 facility in an amount exceeding 75,000
 pounds per year or otherwise used in an
 amount exceeding 10,000 pounds per year.
 For calendar years 1988 and 1989 (and
 beyond), the threshold reporting quantity for
 manufactured or processed chemicals drops
 to 50,000 and 25,000 pounds per year,
 respectively.
   This document has been developed to
 assist those using roller, knife, and gravure
 coating equipment in the completion of Part
 III (Chemical Specific Information) of the
Toxic Chemical Release Inventory Reporting
 Form. Included herein is general information
 on toxic chemicals used and process wastes
generated, along with several examples to
demonstrate the types of data needed and
various methodologies available for esti-
mating releases. If your facility performs
other operations in addition to coating, you
must also include any releases of toxic
chemicals from these operations.
             Step One
  Determine if your facility processes or
   uses any of the chemicals subject to
       reporting under Section 313.
   A suggested approach for determination
of the chemicals your facility uses that could
be subject to reporting requirements is to
make a detailed, review of the chemicals and
materials you have purchased.  If you do not
know the specific ingredients of a chemical
formulation, consult your suppliers for this
information. If they will not provide this
information, you must follow the steps
outlined to handle this eventuality in the
instructions provided with the Toxic Chemi-
cal Release Inventory Reporting Form.
   The list presented here includes chemi-
cals typically used in coating operations that
are subject to reporting under Section 313.
This list does not necessarily include all of
the chemicals your facility uses that are
subject to reporting, and it may include many
chemicals that you do not use. You should
also determine whether any of the listed
chemicals are created during processing at
your facility.
   Solvents: Approximately 50 solvents are
   on the Section 313 list; these include
   1,1,2-trichloroethane, n-butyl alcohol,
   ethylene glycol, methyl ethyl ketone,
   2-ethoxyethanol, xylene, and toluene

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   Pigments: Primarily metal-containing
   compounds such as titanium dioxide,
   zinc oxide, white lead, barium sulfate,
   chromium oxide, nickel titanate, and
   cobalt chromite
   Additives:  Curing agents, surfactants,
   defoamers, thickeners, film control
   agents, and plasticizers such as dibutyl
   phthalate, dimethyl phthalate, dioctyl
   phthalate, ammonia, and diethanolamine
   Polymer and resin precursors
   (residues/impurities): Ethyl acrylate,
   formaldehyde, vinyl chloride, vinyl
   acetate, methyl acrylate, acrylic acid,
   acrylonitrile, ethylene glycol, melamine,
   vinylidene chloride, styrene,
   1,3-butadiene, and phenol
             Step Two
  Determine if your facility surpassed the
    threshold quantities established for
  reporting of listed chemicals last year.
   You must submit a separate Toxic Chemi-
cal Release Inventory Reporting Form for
each listed chemical that is "manufactured,"
"processed," or "otherwise used" at your
facility in excess of the threshold quantities
presented earlier. Manufacture includes
materials produced as byproducts or impu-
rities. Toxic compounds that are incorpo-
rated into your products (for example,
pigments, polymer and resin precursors)
would be considered "processed" because
they become part of the marketed finished
product.  Carrier solvents,  degreasing sol-
vents, cleaning agents, and other chemicals
that do not become part of the finished
product would be considered "otherwise
used."
   The amount of a chemical processed or
otherwise used at your facility represents the
amount purchased during the year, adjusted
for beginning and ending inventories.  To
ascertain the amount of chemical in a mixed
formulation, multiply the amount of the
mixture (in pounds) by the concentration of
the chemical (weight percent) to obtain the
amount of chemical processed.
   Example:  Determining whether tolu-
   ene was used in sufficient quantity
   last year to require reporting under
   Section 313.
       During  1987, a coil coating facility
   used two different coating formulas, one
   containing 38 percent toluene (by weight),
   and the other, 25 percent toluene (by
   weight).  "Pure" (98 percent) toluene was
   also purchased for use as a coating
   thinner.  Purchasing and inventory records
   indicate the following:
   •   100,000 pounds of the 38 percent
       toluene coating was purchased in
       1987; 2,000 pounds was in storage at
       the beginning of the year, and 7,000
       pounds was in storage at the end of
       the year.
   •   50,000 pounds of the 25 percent
       toluene was purchased in 1987; 5,000
       pounds was in storage at the begin-
       ning of the year, and none was in
       storage at the end of the year.
   •   25,000 pounds of the 98 percent
       toluene was purchased in 1987; none
       was in storage at either the beginning
       or the end of the year.
   The quantity of toluene used can be
   calculated as follows:
       [(2,000 Ib x 0.38) + (5,000 Ib x 0.25)]
       (beginning inventory) +
       [(100,000 Ib x 0.38) + (50,000 Ib x
       0.25) + (25,000 Ib x 0.98)]
       (purchased) -
       (7,000 Ib x 0.38) (ending inventory)
       = 74,350 Ib
   Because this is in excess of the 10,000-
   pound reporting threshold for "otherwise
   used" chemicals, a Toxic Release Inventory

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    Reporting Form must be completed for
    toluene.
    A listed chemical may be a component of
 several formulations you purchase, so you
 may need to ask your supplier for informa-
 tion on the concentration (percentage) of the
 chemical in each. For chemical categories,
 your reporting obligations are determined by
 the total amounts of all chemicals in the
 category.  For example, if zinc oxide and zinc
 sulfate are used as pigments, the quantity of
 zinc compounds processed is the sum of the
 amounts of ZnO and ZnSO4 present.  For a
 substance such as cobalt chromite (CoCr2O4),
 the amount used must be considered in
 determining whether the threshold is met for
 both cobalt-containing and chromium-
 containing compounds.
   You must complete a report for each
 chemical for which a threshold is exceeded.
The thresholds apply separately; therefore, if
you both process and use a chemical and
 either threshold is exceeded,  you must report
for both activities. If neither  threshold is
exceeded, no report is needed.
           Step  Three
     Identify points of release for the
     chemical(s) subject to reporting.
   An effective means of evaluating points of
release for listed toxic chemicals is to draw a
process flow diagram identifying the opera-
tions performed at your facility.  The figure
below is an example flow diagram for coating
operations. Because each facility is unique,
you are strongly urged to develop a flow
diagram for your particular operations that
details the input of materials and chemicals
and the waste sources resulting from the
operation of each unit.
   The principal potential sources of chemi-
cal release in typical coating operations are:
   •   Releases of volatile organic com-
       pounds from the coating application
       and dryer areas
                                                     SOLID WASTE,
                                                     NONAQUEOUS LIQUID WASTE,
                                                   1 ' AND/OR WASTEWATER
                          Example Flow Diagram of Roll Coating

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   •  Excess coating mix and solvent from
      the cleanup of the coating applicator,
      coating lines, and empty coating
      drums
   •  Transfer from rail cars or tank trucks
      to storage tanks and subsequent
      transfer to processing tanks
   •  Breathing losses from vents on
      storage tanks
   •  Agitation of mixing tanks that are
      vented to the atmosphere
   •  Evaporation of solvent from the coated
      substrate after it leaves the coating
      lines
   •  Wastes from control equipment used
      to reduce air emissions from the
      coating applicator and dryer
            Step  Four
  Estimate releases of toxic chemicals.
   After all of the toxic chemicals and waste
sources have been identified, you can esti-
mate the releases of the individual chemicals.
Section 313 requires that releases to air,
water, and land and transfers to offsite
facilities be reported for each toxic chemical
meeting the threshold reporting values. The
usual approach entails first estimating re-
leases from waste sources at your facility
(that is, wastewater, air release points, and
solid waste) and then, based on the disposal
method used, determining whether releases
from a particular waste source are to air,
water, land, or an offsite disposal facility.
    In general, there are four types of release
estimation techniques:
    •  Direct measurement
    •  Mass balance
    •  Engineering calculations
    •  Emission factors
Descriptions of these techniques are provided
in the EPA general Section 313 guidance
document, Estimating Releases and Waste-
Treatment Efficiencies for the Toxic Chemical
Release Inventory Form.
   Provisions of the Clean Air Act, Clean
Water Act, Resource Conservation and Re-
covery Act, and other regulations require
monitoring of certain waste streams.  If
available, data gathered for these purposes
can be used to estimate releases. When only
a small amount of direct measurement data
is available, you must decide if another
estimation technique would give a more
accurate estimate. Mass balance techniques
and engineering assumptions and calcula-
tions can be used in a variety of situations to
estimate toxic releases. These  methods of
estimation rely heavily on process operating
parameters; thus, the techniques developed
are very site-specific.  Emission factors are
available for some industries in publications
referenced in the general Section 313 guid-
ance document. Also, emission factors for
your particular facility can be developed in-
house by performing detailed measurements
of wastes at different production levels.
   The mass balance technique for esti-
mating emissions is well suited for coating
operations because of the numerous environ-
mental release points involved and the ease
with which the ultimate fate of waste'chemi-
cals can be determined (that is, process
solvents and volatile components of the coat-
ings are released to air, whereas nonvolatile
components of the coating that do not
become part of the product are released as
solid waste or wastewater from clean opera-
tions).  Direct measurement of waste sources
is applicable in any situation; however, such
measurements are not routinely performed
for many of the coating chemicals subject.to
reporting.
    To estimate toxic chemical releases by
mass balance, one must know the  quantity of
chemical purchased (adjusted for changes in
inventory) and the quantity retained in the
coated product. The difference in these two

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 quantities yields the amount of chemical
 released as waste. An engineering assump-
 tion is then used to determine the method of
 release (air emission, wastewater, solid
 waste). For coating operations, the following
 assumptions can be used:
    •  All volatile organic compounds
       present in the applied coating formu-
       lation, such as solvent coating
       carriers and unpolymerized resin
       precursors, can be assumed to be
       released as air emissions.
    •  The portion of nonvolatile compounds
       in the coating formulation that is not
       retained on the coated substrate can
       be assumed to be released during
       cleaning as solid waste (including
       nonaqueous liquid waste) or waste-
       water, depending on the cleanup
       method.
    •  All solvents used during cleanup of
       coating equipment can be assumed to
       end up as solid waste (nonaqueous
       liquid waste) and/or air emissions,
       depending on the cleanup method.

 Toxic Releases to Air
    The mass balance approach is easily
 applied to solvent carriers of coating solids
 because they are purposely volatilized during
 coating and drying.  Therefore, the quantity
 purchased (adjusted for inventory changes) is
 the quantity released to air.  If a control
 device is used, the quantity of the solvent
 released should be adjusted for removal
 efficiency.  If solvent is recovered from the
 control device and reused (as a carrier) in the
 process, the total quantity of solvent released
 to the air will still be equal to the quantity of
 solvent purchased, adjusted for inventory
 change (because the solvent recovery is an
 internal reuse, and the benefit of the control
 device manifests itself in a reduction in the
quantity of solvent purchased). If the re-
covered solvent is shipped offsite instead of
being reused, the quantity of solvent released
to air would equal the difference between the
quantity used (quantity purchased adjusted
 for inventory change) and the quantity re-
 covered. In this case, the quantity recovered
 would be reported as "transferred to offsite
 locations."

    In some coating processes, a small
 amount of solvent may be retained in the
 product. Although this is usually a negligible
 amount, if a rough value of the quantity
 retained is known, it can be subtracted from
 the quantity released to air.

    Unpolymerized resin precursors are
 usually present in small quantities in organic
 coating formulations. Typically, these com-
 pounds are highly volatile and will be re-
 leased to air during drying.  The entire
 quantity present in the purchased coating
 (adjusted for inventory changes) can be
 assumed to be emitted to air.  Amounts of
 chemicals in purchased formulations in
 concentrations below the 1% de minimis level
 (0.1% for carcinogens), however, do not have
 to be considered in threshold calculations.
Again, if a control device is used for the dryer
 and coating area exhaust, its efficiency
 should be factored into the estimated releases
 of these compounds.
   Example: Estimating releases of
   volatile  toxic compounds from a
   coating formulation.
       A direct roll coater is used to apply an
   alkyd-urea-formaldehyde resin top coat on
   plywood paneling. Urea-formaldehyde
   resin makes up 45 percent of the coating
   solids, and according to the manufacturer,
   this urea-formaldehyde resin contains
   1.5 percent free formaldehyde.  The
   density of the coating solids is 10 pounds
   per gatton of solids. As purchased, the
   coating containing xylene has 8 pounds of
   solids per gallon of coating.  Before it is
   applied, the coating is  thinned with xylene
   at the coating facility to yield 4 pounds of
   soUds per gallon of coating.
       According to purchasing and inventory
   records, 10,000 gallons of the purchased
   coating formulation was processed during
   1987. Assuming complete volatilization of

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      QSP » QSR+QSW
      QSP = (dxCTxCA) + QSW
where QSP = total quantity of nonvolatile
             solids in coating processed
      QSR = total quantity of nonvolatile
             solids retained in substrate
     QSW = total quantity of nonvolatile
             solids wastes
         d = density of solids
       CT = coating thickness
       CA = coated area
   A relationship can be used to determine
an overall coating transfer efficiency for an
application/coating combination.
          (QSR+QSP)=te
          QSP x te = QSR
          QSPx(l-te) = QSW
where te = overall transfer efficiency
   For an individual toxic compound present
as a nonvolatile solid,  the overall transfer
efficiency can be used to make a direct
estimate of releases from the quantity of the
chemical in the purchased coating (adjusted
for inventory changes).
       QCP x (1 - te) = QCW
where QCP =  quantity of nonvolatile solid
               chemical processed
      QCW =  quantity of nonvolatile solid
               chemical wasted
   Example: Using a mass balance to
   estimate releases of nonvolatile toxic
   compounds from coating formulations.
       A roll coater applies a water-based
   polyester resin paint to metal coil  The
   formulation contains titanium dioxide
    CTiOJ and white lead (PbCOJfor coloring.
   According to Information provided by the
    manufacturer, the paint contains 14.5
   pounds of nonvolatile solids per gallon of
    coating, and the density of the solids is
    15.3 pounds per gallon. Also, the titanium
    dioxide and white lead represent 32 and
 19 percent by weight of the nonvolatile
 solids. EPA has proposed to remove TiO2
from the Section 313 list; however, this
 example is also representative of the use of
 a mass balance to estimate releases of
 other similar compounds.
    Purchasing and inventory records
 indicate that 39,000 gallons of this
formulation was processed during 1987.
 Production records indicate that
 13,200,000 square feet of coil received a
 3-mil coat of this formulation. The roll
 coater is cleaned with a water wash, and
 the resultant wastewater is discharged to
 the local sewers.  The quantity ofTiO2 and
 Pb released via wastewater can be
 estimated by the following calculations:
 Amount of nonvolatile solids processed =
    39,000 gal coating x
    10.5 Ib solids/I gal coating
    = 409,500 Ib
 Volume of solids applied to coil =
    13,200,000 ft2 coil x
    0.003 in. thickness +
    12 in./1 ft x
    7.48 gal/IJt?
    = 24,684 gal
 Amount of solids applied to coil =
    24,684 gal solids x
    15.3 Ib solids /I gal solids
    = 377,665 Ib
 Coating solids transfer efficiency =
    377,665 Ib (appUed) •*•
    409,500 Ib (processed)
    = 0.933
 Amount ofTiO2 processed =
    409,500. Ib (solids processed) x 0.32
    (TiO2 wt. percent)
    = 131,040 Ib
                                             8

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    Amount ofTiO2 released =
       131,040 Ib processed x(l- 0.933)
       = 8,780 Ib
    Amount o/PbCO3 processed =
       409,500 Ib (solids processed) xO.19
       (Pb wt. percent)
       = 77,805 Ib
    Amount ofPb released =
       77,805 Ib PbCO3 processed x
       (1 - 0.933) x
       1 mole PbCO3/267 Ib PbCO3 x
       207 Ib Pb/1 mole PbCO3
       = 4,041 Ib
    Because the wash water leaves the facility
    through local sewers, 8,800 pounds ofTiO2
    and 4,000 pounds ofPb would be reported
    as "discharged to POTW."- If the roll coater
    was cleaned by a "dry" method and the
    cleanup wastes were drummedfor
    shipment to a waste recovery or disposal
   facility, the same calculations would apply
    and the amounts would be reported as
    "transferred to an off site location."

Toxic Releases Via Solid Waste
   As mentioned in the preceding sections,
solid and nonaqueous liquid wastes are
generated in "dry" coating cleanup opera-
tions.  These wastes contain cleanup solvents
and nonvolatile coating solids that were not
transferred to the substrate.  The mass
balance techniques demonstrated in the
example concerning cleanup operations are
also applicable to releases via solid and
nonaqueous liquid wastes.
   Toxic chemical releases via solid and
nonaqueous liquid wastes may be measured
directly by using data gathered for com-
pliance with RCRA regulations.  Many spent
solvents are listed as hazardous waste under
RCRA Waste Codes F002 through F005.
These codes may apply to spent solvents used
 to clean up the coating applicator and
 surrounding area. Many spent cleanup
 solvents may also be considered hazardous
 under RCRA because of EP toxicity or ignition
 characteristics.
    The RCRA manifesting procedure for
 hazardous waste shipped offsite requires
 documentation of quantities shipped.  Treat-
 ment, storage, and disposal facilities must
 perform detailed chemical and physical
 analyses on the wastes. The waste also may
 be analyzed at your facility. Therefore,
 estimates of releases for several compounds
 can be made by direct measurement.

 Other Toxic Releases
    Coating operations produce other wastes
 from which toxic chemicals may be released.
 These include:
    •   Residues from pollution control
       devices
    •   Product rejects
    •   Used equipment
    •   Empty chemical containers
    Releases from these sources may already
 have been accounted for, depending on the
 release estimation methods used. These
 items (and any other of a similar nature)
 should be included in your development of a
 process flow diagram.
    The contribution of sources of wastes
 such as cleaning out vessels or discarding
 containers should be small compared with
 process losses. If you do not have data on
 such sources (or any monitoring data on
 overall water releases), assume up to 1  per-
 cent of vessel content may be lost during
 each cleaning occurrence.  For example, if
you discard (to landfill) "empty" drums  that
 have not been cleaned, calculate the release
 as 1 percent of normal drum content.  If the
 drums are washed before disposal, this may
 contribute 1 percent of the content to your
wastewater loading.
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vvEPA
United States
Environmental Protection
Agency


Office of Pesticides and
Toxic Substances, WH-562A
Washington, D.C. 20460
Official Business
Penalty for Private Use
$300

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