E?/l-6QO/2-76-032a
February 1978                         Environmental Protection Technology Series
                                    SOURCE ASSESSMENT:
                                                  £
                               PRIORITIZATJON OF STATIONARY

                                     AIR POLLUTION SOURCES-

                                            MODEL DESCRIPTION

                                                  —••---•
                                     industrial Environmental Research Laboratory
                                           Office of Research and Development
                                          U.S. Environmental Protection Agency
                                     Besearsh Triangle Park, North Carolina 27711

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                            EPA-600/2-76-032a
                            February 1976
            SOURCE ASSESSMENT:

        PRIORITIZATION OF STATIONARY

  AIR  POLLUTION SOURCES—MODEL DESCRIPTION
                    by

             Edward C. Elmutis
       Monsanto  Research Corporation
             1515  Nicholas Road
            Dayton, Ohio  45407
          Contract  No. 68-02-1874
             ROAP No. 21AVA-003
         Program Element No.  1AB015
     EPA Project  Officer:  Dale A. Denny

Industrial  Environmental Research Laboratory
  Office of Energy, Minerals, and Industry
      Research  Triangle  Park, NC  27711
                Prepared  for

    U.S.  ENVIRONMENTAL  PROTECTION AGENCY
     Office of Research and Development
           Washington,  DC 20460

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                          PREFACE
The Industrial Environmental Research Laboratory (IERL)  of
EPA has the responsibility for insuring that air pollution
control technology is available for stationary sources.
If control technology is unavailable, inadequate, uneconomical
or socially unacceptable, then development of the needed
control techniques is conducted by IERL.  Approaches
considered include process modifications, feedstock modifi-
cations, add-on control devices, and complete process
substitution.  The scale of control technology programs
range from bench to full scale demonstration plants.

The Chemical Processes Branch of IERL has the responsibility
for developing control technology for a large number  (>500)
of operations in the chemical and related industries.  As
in any technical program the first step is to identify the
unsolved problems.

Each of the industries is to be examined in detail to
determine if there is sufficient potential environmental
risk to justify the development of control technology by
IERL.  As a first step, Monsanto Research Corporation (MRC)
has developed a priority listing of the industries in each
of four categories:  combustion, organic materials, inor-
ganic materials, and open sources.  The purpose and intended
use of this listing is that it serve as one of several
guides to the selection of those sources for which MRC will
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perform detailed source assessments.  Source assessment
documents will be produced by MRC and used by EPA to make
decisions regarding the need for developing additional control
technology for each specific source.

Prioritization listings were developed to aid in the selection
of specific sources of air emissions for detailed assessment.
This report describes the general prioritization model, the
manner and form of its implementation, and detailed examples
of use.

This prioritization work was initiated under Task XIV,
Development of Source Assessment Documents, of Contract
68-02-1320, Quick Reaction Engineering and Technical Services
(Multiple Option Services Contract); it was continued and
completed under Contract 68-02-1874, Source Assessment.
                              IV

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                         CONTENTS  -
Section                                                Page
I    Introduction                                        1
II   Model Development and General Structure             3
     A.   Mathematical Structure                         6
     B.   Assumptions and Limitations                   10
     C.   Application of the Model                      13
          1.   Derivation of the Ground Level           13
               Concentration
          2.   Data Availability and Computational      15
               Form
               a.   Population Sensitive Calculations   16
               b.   Location Sensitive Calculations     17
               c.   Detailed Input Calculations         18
               d.   Open Source Calculations            18
          3.   Uncertainty Levels                       19
          4.   Prioritization Sensitivity Analyses      20
          5.   Priority Listings of the Four            23
               Categories:  Combustion, Inorganic
               Materials, Organic Materials, and
               Open Sources
III  Appendixes - Detailed Examples Using               35
     Prioritization Model
     A.   Use of Model with Common Inputs               36
     B.   Example of Population Sensitive Calculation   40
     C.   Location Sensitive Calculation                50
     D.   Example of Detailed Calculation               58
     E.   Example of Open Sources Calculation           67
IV   References                                         75

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                           TABLES
Table

  1


  2


  3


  4

  5
Effect of Changes in Input Variables
on Impact Factor

Prioritization Listing - Combustion
Sources

Prioritization Listing - Inorganic
Sources

Prioritization Listing - Organic Sources

Prioritization Listing - Open Sources
Page

 21


 24


 25


 27

 32
Figure

  1
                           FIGURES
Acrylonitrile Impact Factor vs. TLV
(Organics)
Page

 22
                             VI

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                         SECTION I

                       INTRODUCTION
This report provides:  a general description of the priori-
tization model and the various factors that it can incor-
porate; a description of the actual application of the model;
a description of the types of calculations that were per-
formed depending upon the degree of input aggregation; the
results of sensitivity analyses to show how the prioritization
model responds to changes in input; and, detailed examples
of use of the model.

The relative rank ordering or prioritization of source types
was accomplished by computing a relative environmental
impact factor for each source type.  A source type is
defined as an operation, process, combustion method, or
industry that emits common species and has similar emission
factors for those species.  For example, acrylonitrile
manufacturing, coal-fired utility boilers, glass manufacturing,
beef cattle feed lots, and open mining of coal represent five
different source types.  To date, over 600 source types have
been identified.

In its implemented form, the prioritization model has taken
several aspects.  Because of a time constraint and due to
the size of the data base, it was necessary in many cases
to aggregate the input data.  Regardless of the degree of
data aggregation, the basic form of the prioritization
                             1

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model was identical in all cases; only the level of detail
in the input was altered.

This model does not attempt, in any fashion, to relate
industrial emissions to their effect on public health.
Based upon a set of common assumptions, which are clearly
identified, the model provides a relative rank ordering
(within the framework of these assumptions) of stationary
sources of air pollution.  A priority listing was developed
for each of four categories:  combustion, organic materials,
inorganic materials, and open sources.  Four priority
listings were produced since all of the source types could
not be grouped into one category.  Differences in the nature
of the emissions which result from broad dissimilarities in
fuel consumption patterns and/or types of products manufactured
precluded this.

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                        SECTION II

          MODEL DEVELOPMENT AND GENERAL STRUCTURE
The basic proposition of this prioritization model is that
emission sources can be ranked,  based upon the potential
degree of hazard that they impose upon individuals in their
environment.  This degree of hazard can be expressed in
different ways.  A traditional method of expressing degree
of hazard has been to use the mass of emissions from various
source types.  Other techniques have used ambient air
contributions of a given source type and the resulting
degradation of ambient air quality as an indicator of source
severity.

The air pollution severity of a given source should in some
way be proportional to the degree of potential hazard it
imposes upon individuals in its environment.  The relative
hazard, H, from a specific emission can be defined as being
proportional to the ratio of the delivered dose to the
toxicity of the material, probability of dose delivery, and
number of people who would receive it as follows:
                             L
                             LD50
where     N = number of persons
            = lethal dose for 50% of the people exposed
          P = probability of dose delivery

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          T = delivered dose = B'R-/x(t)dt
          B = average breathing rate
          R = lung retention factor
       X(t) = concentration time history
A relative or potential hazard, H ,  is defined as the ratio
of the dose of the pollutant delivered to a population,
relative to some potentially hazardous dose.  Since LDso
data are not available for human beings, another measure of
potentially hazardous dosage was used.

The potentially hazardous dose for a given pollutant from a
specific point source in a given region is thus defined as
follows:
                         r2  '
               ¥F = NBR  /  TLV(t) K dt                 (2)
                        tl
where   ^  = potentially hazardous dose, g
             population exposed to a specific source, persons
             average breathing rate, m3/sec-person
             lung retention factor for the pollutant of
             interest  (dimensionless factor, 0
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Similarly, a hazard potential factor, F, is defined as:

                         F = TLV-K                      (4)

Since TLV is a constant,

                    *_, = N'B'R'T-F                      (5)
The actual pollutant dose delivered, Ya, from a given point
                                      A
source can be calculated as follows:
                                 r2
                       = N-B-R   /  x  (t) dt             (6)
where  x(t) = tne actual ground level concentration  time
              history of a pollutant of interest emitted by
              a specific point source, g/m3
The value of \(t) is very difficult to obtain and was  there-
fore approximated by an average value, x".   (Procedures for
obtaining x are discussed in a later section of  this report.)
The total actual dose delivered for a specific pollutant
from a specific source is then:

                    V  = N-B'R'T'x"                      (7)
                     f\

Since our measure of potential source hazard, H_, was  defined
as the ratio of the two dosages, then:
                         w
                          A   N«B«'R«lTl«
                              N'B'R'T-F
or                  Hp = X                   .           (9)

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A.
     MATHEMATICAL STRUCTURE
The relative degree of hazard or potential hazard created
        ^ 1.                                    ^ l_
by the i — material in the region around the j — source is
expressed as the ratio of x"
                            . .
                              to F., i.e.,
               Degree of hazard =
                                  F.
                                                       (10)
In a similar manner, it may be stated that there already
exists some ambient level, x1-•/ °f tne i— material at the
 th                          x^
j— source.  If there is an ambient air quality standard,
S., for this emission then a weighting factor, W.., is
defined as follows:
                     r^  when   s •> > 1.0
                     'i           i

                               X'i:i  .
                     1.0 when   „ J _ 1.0
                                                        (11)
                     1.0 when  S. is undefined  (i.e.,  for
                                1 non-criteria  pollutants)
For the purpose of this prioritization study, particulates,
sulfur oxides, nitrogen oxides, hydrocarbons and carbon
monoxide were designated as criteria pollutants.  Oxidants
are not included in that category because  they  are  not
emitted from point sources but instead are formed from
nitrogen oxides and hydrocarbons released  to the atmosphere,

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If the degree of hazard, ^—L, in equation 10  is multiplied



by the population density,  P., in the region  around  the  j —



source, a measure of the severity, SV.^., imposed on  individuals

        * y^                  ^l-

by the i— material at the  j— source, is obtained:
                     Ai-
Severity = SV. .  = P. ==-
             iJ     D  i
                                                       (12)
         .th
For the j— source, the severity vector,  SV.,  is defined  by:




                                       /    V^
      SV. =
                                           Fi
                                        P.  *Nj
                                                       (13)
where  N = number of emitted species.  The existing  criteria

standard or weight vector, W., is defined by:
   W. =
                                   X
                                                       (14)

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Ideally, at the j— source the severity vector should be zero.
Thus, to get a measure of the severity associated with the
j— source, the Euclidean distance is computed between the
calculated severity vector, SV., and the zero vector,
weighted by the ratio of ambient criteria level to the
standard vector, W..  This distance is also referred to as
the length of SV. and is given by:
        Length of SV. =
                                    N
                    SV .2 W..I1/2
                                   i=l
                    (15)
or.
sv.| I  = P..
                                               1/2
                                                       (16)
The next step is to assign some numerical value called
the impact factor, I  , to the original source type x in
                    X
such a way that the impact factors for different source
types can be compared and ranked.  One possible method is
to let the impact factor be the largest of the lengths of
the severity vectors associated with the sources j = 1,
     K
      x'
         i.e.
               I  = max
                A
       |SV.
D ~
K
                                               x
(17)
However, this assigns a high impact factor to a source type
that severely pollutes from one point source and has little
or no pollution from all other point sources within that
source type.

Another possible method of assigning impact factor values
is to let Ix be the mean of the lengths of the severity
vectors.  However, this definition suffers from the varying
                              8

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number K  of point sources in the different source types.
        vt
For example, if K  =10 for one source type and all severity
                 J\
vectors have unit length, then their mean would be 1, and
I  would have a value of 1.  On the other hand, if K  = 100
 X                                                  X
for another source type and all the severity vectors in
this source type are also of unit length, then again the
mean value would be 1 and I  would have the same value as
                           J^
before.  However, it is reasonable to assume that the
latter source type should have more impact on the environ-
ment than the former.
Accordingly, the impact factor, I , associated with a given
                                 X
source type x is defined to be the sum of the lengths of
the individual severity vectors associated with the point
sources within the source type.  Thus:
I. =
                       N
                                       1/2
                                                        (18)
where    I  = impact factor, persons/km2
          *i
         K  = number of sources emitting materials associated
              with source type x
          N = number of materials emitted by each source
         P . = population density in the region associated
          -*   with the j_ source, persons/km2
        X- . = calculated maximum ground level concentration
          ^   of the ii£ material emitted by the jHl source,
              g/m3
         F. = environmental hazard potential factor  of  the
          1   iih material, g/m3
       X ' . . = ambient concentration of the  i — material in
          -1
              the region associated with the  jl source
         S . = corresponding standard for the  i — material
          1   (used only for criteria emissions, otherwise
              set equal to one)

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B.   ASSUMPTIONS AND LIMITATIONS

In this study, the prioritization model was to be computer-
ized, all data handling programs were to be written, and
all input data were to be collected and processed within a
period of three months.  The input data in this case meant
descriptions of all stationary air pollution sources in the
United States.

Before discussing the actual application of the model, it is
appropriate to restate the objectives of the prioritization
model, list the elements that it can treat, and indicate
the elements that were specifically excluded.  (It is not
within the scope of this report to provide an exhaustive
list of all the things that the model cannot do or was not
intended to do.  Some objections have been raised regarding
various structures and procedures, and these will be addressed
in the best way possible without trying to be exhaustive
and without trying to anticipate every objection possible.)

The prioritization model was designed to rank order source
types in each of four predetermined categories:  organic
materials, inorganic materials, combustion, and open sources.
A concentrated effort was expended to obtain individual
category listings for the purpose of providing a basis on
which to select areas for future assessment.  This means
that if in a given priority listing, Source Type A has an
impact factor one order of magnitude higher than Source
Type B, this does not indicate that any health problems
associated with Source Type A are one order of magnitude
more severe than those associated with Source Type B.
What it does indicate is that within the level of uncertainty
in the input data, Source Type A has a potentially greater
impact on the environment than Source Type B.  Th.e difference
in impact factor values cannot be quantitatively interpreted

                             10

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since this model gives only a relative ranking of source
severity.

Some of the factors that the prioritization model is
capable of treating in the list of sources developed are
shown below :

          a varying number of air pollutants emitted by
          a given source type
          the  hazard potential of emitted particles
          production capacity associated with an emission
          factor to yield emission rates
          varying heights of emissions
          population density in the region of a source
          existing ambient concentrations of emitted
          materials
          local meteorological data
          distances from source to receptors  (populated
          areas)
          measured or estimated emission rates
          growth or decline of source types
          measured ambient air concentrations of
          emitted materials
          atmospheric decay of emitted materials

While the model structure is capable of treating the above
factors, not all of them were used in the initial prior-
itization.  Those inputs that were used are identified
explicitly in Section II.C.

There are certain clarifying points to be made regarding
the model structure and the inclusion of specific terms.
The safety factor, K =  [(40/168)(1/100)], is used to compensate
for the fact that TLV's were established for a five day
work week exposure, and that the general population is a
higher risk group than healthy workers for which the TLV
values were established.  Since this factor is constant for

                             11

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all emitted species, and for all source types, its inclusion
into the prioritization model does not affect the ranking.
It was kept, however, to preserve computational commonality
with other forms of equations that were developed later for
describing source severity.

The model does not account for differences in dose/response
relationships between pollutant agents; rather, a linear
relationship for all materials is assumed.  Since the
prioritization model and resulting listings are only one of
many management tools being used by EPA in the source
assessment program, it was not felt that the detailed
investigation of dose/response relationships would be
beneficial at the time.  The model assumes additivity of
effects, a technique recommended by ACGIH.

The model does not account for air pollutant persistence,
long range transport, and transformation characteristics.
Based on the objectives of the prioritization effort and
the time constraint, it was thought that the data base used
to define the atmospheric transformations and long range
transport of a wide variety of pollutants was not sufficiently
developed to be usefully included.  In a subsequent section
of this report, a procedure is described for asking questions
about the effect of changes in emitted materials based on
the use of sensitivity analysis.  Specific examples of this
approach include the conversion of all emitted S02 to
sulfate  (using the sulfate TLV), and the conversion of all
hydrocarbons to photochemical oxidants  (using the photo-
chemical oxidant TLV).
                            12

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C.   APPLICATION OF THE MODEL

1.   Derivation of the Ground Level Concentration

Determining the ground level concentration, x» requires the
use of a dispersion model.  The simple Gaussian Plume
equation for ground level receptors at the plume center-
line was used:1
              X =
Q
                                               *
                                   (19)
where   x = ground level concentration, g/m3
       a  = lateral dispersion coefficient, m
       a  = vertical dispersion coefficient, m
        h = effective emission height, m
        Q = emission rate, g/sec
        u = wind speed, m/sec
        x = distance from source to receptor, m
        X = decay constant, sec"1

The dispersion coefficients are power law functions of
downwind distance and atmospheric stability:2
                    o  = ax0-9031                       (20)
                    cr = bxc + d                        (21)
turner, D. B.  Workbook of Atmospheric Dispersion Estimates,
 Publication No. 191482, May 1970.
2Eimutis, E. C., and M. G. Konicek.  Derivations of Continu-
 ous Functions  for the Lateral and Vertical Atmospheric
 Dispersion Coefficients.  Atmospheric Environment, 6:859-
 863, 1972.
                             13

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Coefficients a, b, c, and d were derived for the various
stability categories.2

It was noted that compiling data on distances from sources
to receptors would not prove feasible.  Hence, there
remained atmospheric stability, wind speed, and decay
constants as required inputs.  After a review of the priori-
tization objectives and projected use of the prioritization
listings, it was decided that decay constants would not be
used, and that constant average values would be used as input
for wind speed and atmospheric stability.

Since emission height data were compiled, the maximum
ground level concentration, X   , was computed from the
following:3
                                2Qa
                       Xmax =	                  (22)
where  Q = emission rate, g/sec
       e = base e = 2.72
       u = wind speed, m/sec
       h = emission height, m
For neutral or slightly unstable conditions, a  = a ,3
and:
                         i»i
The national average wind speed was used as a constant
input  (approximately 10 mph or 4.5 m/sec).  The average
3Slade, H. S.  (ed.).  Meteorology and Atomic Energy.  Publi-
 cation TID 24190, July 1968.
                             14

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concentration, x» is a function of sampling time, t, and
can be related to the maximum concentration, x   » by the
                                              UlciX
following:1
                    X « Xmax t-                         (24)

where  0.17 < p < 0.2

Since a relative rank ordering was being performed, the
choice of constants d
was used directly for
choice of constants did not affect the ordering and x
                                                     max
The buoyancy and momentum data needed to estimate plume
rise could not be compiled within the project time  frame.
The emission height thus corresponds to the physical and
not the effective emission height.  Fall-out, washout,
surface adsorption and vegetative absorption were not
included  in the implemented model.

2.   Data Availability and Computational Form

Data availability can be summarized in two categories:   little
or no data available for a given source type; or, thousands  of
pages of  computerized printout of point source  information.
It was quickly evident that,  for the latter case, some  form
of input  data aggregation would have to be performed.

It should be noted that the basic model structure was not
changed;  only the level of detail was altered for those
source types with emission points numbering in  the  thousands
•and, in some cases, in the hundreds of thousands.   Four
types of  calculations and procedures were implemented:
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          Population sensitive calculations - Examples
          include industrial boilers, asphalt plants,
          ready-mix concrete plants, etc.  These industries
          were assumed to be located, preferentially, in
          areas of higher population or distributed accord-
          ing to population fraction.
          Location sensitive calculations - Examples include
          cotton gins, mining operations, etc.  These
          source types are located only in certain areas
          of the country.

          Detailed source calculations - These are the source
          types with only a small (less than 10)  number of
          plants.  An example is acrylonitrile manufacturing
          plants.  In this case, the prioritization model
          in it's detailed form was used.  Each plant was
          included as a separate point source.

          Open source calculations - These source types were
          categorized as population sensitive, area sensitive,
          or location sensitive.  Separate programs were
          written to deal with the differing inputs which
          the open sources calculation required.


a.   Population Sensitive Calculations


For population sensitive calculations, the population fraction

of each state was taken from the 1970 Census.  The national

yearly capacity or fuel consumption for a given source type

was then distributed as follows:
                         PF  =                           (25)
where  PF . = population fraction in the j — state

        P . = population of the j — state
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Then, for the i — pollutant,

                    Qij = I  (Kf) (EiHPF.) (CAP)         (26)

where  Q. .  = emission rate, g/sec
         f = frequency of operation, days/365 days
        E.  = emission factor, Ibs of i — emission/tons of
             product or fuel
       CAP = national yearly capacity or fuel consumption,
             tons
        K, = conversion factor (Ibs/year to g/sec)

The frequency factor was included since many industries and
operations exist that are intermittent or seasonal.  If a
process operates for 100 days out of a year, then the
emissions rate is 3.65 times higher than it would be if one
had assumed continuous yearly operation.
Ambient air averages for the criteria pollutants were used
for each state and the model was exercised as previously
described.  A full listing of the state data base is pre-
sented later in Tables A-l and A-2 of Appendix A.

b.    Location Sensitive Calculations

For some source types, capacity information was available
on a state by state basis.  For example, for coal-fired
steam electric utilities, data are published on fuel consump-
tion on a state basis.  Knowing the capacity and its dis-
tribution across the states for each emission, the emission
rate is calculated as follows:
                              (Kf) (E^ (CAP..)  .          (27)
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The impact factor is then calculated in the usual fashion
and summed over K  states.
                 J\.

c.   Detailed Input Calculations

Detailed input calculations were segregated by county for
population densities.  Since the county ambient air summaries
were not available, corresponding state values were used.
Individual plant capacities were used to calculate the
emission rates and the summation extended over the number
of plants in a given source type.

d.   Open Source Calculations

Open source calculations were further divided into three
types:   (1) population sensitive, (2) area sensitive, and
(3) location sensitive.  Population sensitive calculations
were performed as previously described.  Area sensitive
calculations were performed using:

                    AF  = 5!                            (28)
where  AF . = area fraction of the j — region or state
        A. = area of the j — region or state, mi2
Then,
                     j = j  (CAP) (Ej) (AFj) (Kf)           (29)
and the national capacity is apportioned according to area
Open source location sensitive calculations were performed
as previously described.
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These descriptions of the various calculation methods have
been brief and are meant to serve as an introduction.  Detailed
examples of their use are included in the Appendix.

3.  Uncertainty Levels

There is a level of uncertainty associated with each impact
factor.  While that level cannot be quantified, it can be
assumed to vary as a function of the quality of available
information on a specific source type.  Using this rationale,
the priority index uncertainty levels were defined as follows:

               Level          	Meaning	
                 A            Adequate data of reasonable
                              accuracy
                 B            Partly estimated data of
                              indeterminate accuracy
                 C            Totally estimated data of
                              indeterminate accuracy
                 D            Missing data on known emissions
                              of toxic substances

• Example of Level A - Adequate data of reasonable accuracy
are available for the gas-fired steam electric utilities.
Emissions are known and emission factors are published for
this industry.

• Example of Level B - Partly estimated data are available
for oil-fired industrial/commercial boilers.  These data
represent best engineering estimates.

• Example of Level C - Totally estimated data are the type
available for the emissions from all types of structural
fires.
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. Example of Level D - If it is known that a source is
emitting asbestos, mercury, beryllium, cadmium, POM's,
benzenoid aromatics, or other suspected carcinogens and yet
no quantitative data for such emissions are available, then
that source type has an uncertainty level of D.  Coal refuse
piles - open burning is an example of this level of uncertainty.

The above defined uncertainty levels are subjective.  They
were assigned by the individual responsible for generating
data for a specific source type.  Even with the lowest un-
certainty level, Level A, attempts to quantify the uncertainty
would present a formidable task.  However, sensitivity analyses
were performed on the prioritization model in order to observe
its response to changes in the inputs.  These results are
discussed in the following section.

4.   Prioritization Sensitivity Analyses

The sensitivity, AI , of the impact factor, I  , to changes
                   x                         x
in various inputs was defined as:
                   = ioo( x(new) - Ix(base) J
                         \       I _ /i	\     /
                       (30)
x(base)
where  Ix(t,ase) = imPact factor based on original input
        Ix(new) = imPact factor based on revised input

Coal-fired steam electric utilities were selected as an
example source type for thi's sensitivity analysis.  In the
calculation, one input variable at a time is either increased
or decreased by a constant factor and the percent AI  is
                                                    X
noted.  This process was performed on several of the input
variables.  The following table summarizes the variables
altered (Z), and the corresponding percent changes in the
impact factor.

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      Table 1.  EFFECT OF CHANGES IN INPUT VARIABLES
                     ON IMPACT FACTOR
   Input variable  (Z )
AI (%) when input
variable is 1.5 Z
AI (%) when input
variable is 0.5 Z
Frequency
Wind speed
TLV
Criteria standard
Emission height
Emission factor
Criteria concentration
Capacity
Population density
       -33.3
       -33.3
       -33.3
       •18.4
       •55.6
       50.0
       22.5
       50.0
       50.0
      100.0
      100.0
      100.0
       41.4
      300.0
      -50.0
      -29.3
      -50.0
      -50.0
In another test of sensitivity, the effect of pollutant
transformation was investigated.  The specific example was
the conversion to sulfate of all S02 emitted by a coal-
fired electric utility.  Using TLV's as indicators of
sensitivity, the following results were computed:

S02
Sulfate
TLV, g/m3
0.014
0.0042
I (normalized)
J\
100
247
In this case, a 70% decrease in TLV value produced a 147%
increase in the impact factor.

In another instance, questions were raised concerning S02
emission factors.  The impact factors for coal-fired
utilities were computed with a base-line emission factor
and with a factor three times higher  (i.e., 200% increase)
The impact factor showed a corresponding 190% increase.
                             21

-------
Another example of  sensitivity  was  shown using acrylonitrile
manufacturing as an example.  By varying the TLV's of three
emissions  (acrylonitrile,  propane,  and propylene)  the results
shown in Figure 1 were obtained.
         10»r
          10'
          106
10

10
                           TIV, g/m
                                            10
Figure 1.  Acrylonitrile  impact factor vs. TLV (organics)
                             22

-------
5.   Priority Listings of the Four Categories:  Combustion,
     Inorganic Materials, Organic Materials and Open Sources

Several data management routines were written in FORTRAN IV
and these were interfaced with impact factor calculation
routines, sorting, file manipulation and reporting programs.
Priority listings were produced for the combustion, inorganic
materials, organic materials, and open sources categories and
these are presented in Tables 2 through 5.  The column labeled
"UL" refers to the uncertainty level as described earlier
in Section II.C.3, and the column labeled "CALC" refers to
the type of calculation used as described earlier in Section
II.C.2.

               CALC                Meaning
                 1       Population sensitive calculation
                 2       Location sensitive calculation
                 3       Detailed input calculation
                 4       Open source calculation
                               23

-------
      Table  2.    PRIORITIZATION  LISTING  -  COMBUSTION  SOURCES
                                  COMBUSTION SOURCES
          SOURCE TYPE

COAL REFUSE PILES.  OUTCROPS AND ABANDONED NINES
PRESCRIBED BURNING
AGRICULTURAL OPEN BURNING
FUEL BURNING ENGINES -  RECIPROCATING '
OIL FIRED INDUSTRIAL/COMMERCIAL BOILERS
FUEL BURNING ENGINES -  TURBINE
COAL FIXED RESIDENTIAL  SPACE HEATING
OIL FIRED RtSIOENTIAL SPACE HEATING
CHARCOAL MANUFACTURE
GAS FIRED RESIDENTIAL SPACE HEATING
SWIMMING POOL HEATING
INDUSTRIAL/COMMERCIAL SPACE HEATING
OIL-FIRED STEAM ELECTRIC UTILITIES
COAL-FIREU STEAM ELECTRIC UTILITIES
GAS FIRED AIR CONDITIONING
GAS FIRED INDUSTRIAL/COMMERCIAL BOILERS
RESIDENTIAL INCINERATION
GAS FIRED LAUNORY DRYING
CHCHARO HEATING
GAS FIRED RESIDENTIAL WATER HEATING
WOOD WASTE INCINERATION
COAL-FIRLLl IiMl'USTMAL/COMMERCIAL BOILERS
WOOD FIRED RESIDENTIAL  SPACE HEATING
INCINERATION OF "TYPE 1" WASTE
RLFUSE INCINERATION/PYROLYSIS - STEAM GENERATION
INCINERATION OF "TYPE 6" WASTE
OPEN BURNING OF INDUSTRIAL WASTE
MUNICIPAL INCINERATION
MUNICIPAL REFUSE/COAL FIRED UTILITIES
INCINERATION OF "TYPE 0" WASTE
JET ENGINE TESTING
GAS-FIRED STEAM ELECTRIC UTILITIES
COVERED WIRE INCINERATION
AUT0800Y INCINERATION
INCINERATION OF "TYPE 2" WASTE
OPEN BURNING OF WOOD WASTE
INCINERATION OF "TYPE H" WASTE
OPEN BURNING OF JET FUEL
INCINERATION OF "TYPE 3" WASTE
INCINERATION OF "TYPE 5" WASTE
DRUM INCINERATION
SEWAGE SLUDGE INCINERATION
ELECTRICAL EQUIPMENT WINDING RECLAMATION
OPEN PIT INCINERATION
HOSPITAL UASTE  INCINERATION
OPEN BURNING OF RAIL CARS
EXPLOSIVES BURNING
BRAKE SHOE DEBONCING
LAND CLEARING - OPEN BURNING
OPEN BURNING OF AUTO BODIES
ON SITE BURNING - OPEN BURNING
MUNICIPAL DUMPS - OPEN BURNING
ROCKET ENGINE
STRUCTURAL FIRES
NATURAL FIRES
IMPACT  FACTOR
                UL  CALC
900.000,000
200,000.000
200,000,000
100.000.000
60,000.000
50.000.000
30.000. 000
10,000.000
6.000.000
s.ooo.ooo
4.000,000
4,000,000
3,000,000
2,000,000
2,000,000
2.000,000
1,000,000
1,000,000
1,000,000
90U.OOO
900.000
900.000
500.000
too, ooo
300, COO
200,000
200,000
100.000
100.000
90,000
70.000
60,000
60,000
30.000
30.000
20,000
20,000
10,000
10.000
9,000
9,000
9.000
9.000
5,000
3,000
2.000
2,000
100







0
c
B
c
B
c
B
B
c
B
c
0
B
B
c
B
c
c
0
a
c
B
c
D
B
0
D
B
0
0
D
A
D
B
0
C
C
D
D
0
D
C
D
0
D
C
0
D







2
2
2
1
3
1
2
2
1
2
2
1
2
2
2
2
1
2
2
2
2
2
2
1
3
1
1
1
3
1
1
2
1'
1
1
2
1
1
1
1
1
1
1
1
1
3
2
1
1
1
1
1
1
1
1
                                             24

-------
         Table  3.    PRIORITIZATION  LISTING

                                   INORGANIC SOURCES
-  INORGANIC  SOURCES
          SOURCE TYPE

COTTON SINS
PRODUCTION OF LEAD STORAGE  BATTERIES
PIG IRON PRODUCTION
COKE MANUFACTURE
BRICK KILNS AND DRIERS
IRON FOUNDRIES
ASBESTOS PRODUCTS
TOBACCO
PRIMARY ZINC SMELTING
SECONDARY LEAD SMELTING AND REFINING
STEEL PRODUCTION
LEAD CARBONATE AND SULFATE  • UNITE LEAD
CADMIUM PIGMENTS - CADMIUM  SULFIDE. SULFOSELENIDE, LITHOPONE
AMMONIA
LE.AO OXIDE • RED LEAD AND LITHARGE - PIGMENTS ONLT
TITANIUM DIOXIDE - PIGMENT
COAL CLEANING PLANTS - THERMAL  DRYING
SECONDARY 2INC SMELTING
COBALT COMPOUNDS - ACETATE*  CARBONATE. HALIDES. ETC.
GLASS INDUSTRY
SILVER COMPOUNDS - N03, DIFLUORIDEi FLUOROBORATE, S04
PRIMARY ALUMINUM PRODUCTION
SULFURIC ACID
PRIMARY LEAD SMELTING AND REFINING
ZINC CHLORIDE - SO DEGREE BAuME*
VITREOUS KAOLIN PRODUCTS
ELECTROLYTIC PRODUCTION OF  CHLORINE
FERROALLOY PRODUCTION
ZINC OXIDE - PIGMENT
REFRACTORIES
LIME KILNS
AMMONIUM NITRATE
SECONDARY ALUMINUM PRODUCTION
FERTILIZERS - BULK BLENDING PLANTS
COPPER SULFATE - PENTAHYORATE
PHOSPHORIC ACID . WET PROCESS
SUEL FOUNDRIES
CALCIUM CARBIDE
POTASSIUM HYDROXIDE
BRASS AND BRONZE INGOT PRODUCTION
MERCURY COMPOUNDS - HALIOES, NITRATES, OXIDES, ETC.
CEMENT
AMMONIUM SULFATE
CC.AL CLEANING PLANTS - PNEUMATIC
BORIC ACID AND BORAX - SODIUM TETRABORATE
SODIUM CHROMATE AND SODIUM  DICHROMATE
SODIUM TRIPOLYPHOSPHATE
MINERAL WOOL
PHOSPHATE ROCK - DRYING, GRINDING, CALCINING
TRIPLE SUPERPHOSPHATES
ALUMINUM OXIDE - ALUMINA
CHLOROSULFOMC ACID - INORGANIC ACIDS
NICKEL SULFATE
AMMONIUM PHOSPHATES
LEAD ARSENATE - ACID ORTHO-ARSENATE - 'BASIC ORTHO-ARSENATE
NITRIC ACID
CHROMIC ACID
ZINC GALVANIZING OPERATIONS
CALCIUM CHLORIDE
SUPERPHOSPHATE - NORMAL
PHOSPHORIC ACIO - THERMAL PROCESS
PHOSPHORUS PENTASULFIDE
MANGANESE SULFATE
POTASSIUM BICHROMATE AND POTASSIUM CHROMATE
SODIUM SILICOFLUORIDE
PHOSPHORUS TRICHLORIDE
IhON OXIDE - PIGMENTS
LEAD CHROMATE - CHROME YELLOW AND ORANGE
PHIMARY COPPER SMELTING
HYDROFLUORIC ACID
SODIUM CARBONATE - SYNTHETIC
PHOSPHORUS - ELEMENTAL
LEAD COMPOUNDS - HALIOES, HYDROXIDES, DIOXIDE, NITRATE, ETC.
FLUORINE
GYPSUM
PHOSPHATE ROCK DEFLUORINATION
ALUMINUM FLUORIDE.
      IMPACT FACTOR
                       UL  CALC
200,000,000
30,000.000
20.000,000
20,000.000
2.000.000
2.000.000
2,000,000
1,000,000
1.000.000
1.000.000
900.000
800.000
800,000
800,000
700,000
500,000
500,000
1*00,000
400,000
000.000
300,000
300.000
300,000
300,000
200,000
200,000
200,000
200.000
200,000
100,000
loo.ooo
100,000
100,000
100,000
100,000
90,000
90,000
90,000
90,000
80,000
60,000
80,000
70,000
60.000
50,000
50,000
to, ooo
to.ooo
40,000
40,000
40,000
30,000
30,000
30,000
30,000
2U, 000
20,000
20,000
20,000
20,000
20,000
20,000
20,000
20.000
20,000
10,000
10,000
10,000
10,000
10,000
10.000
10,000
10,000
10,000
9,000
. 9,000
9,000
B
c
c
D
c
c
B
c
c
0
c
0
c
A
D
B

c
c
A
0
c
B
C
D
C
8
C
B
B
A
B
D
C
C
B
0
B
C
C
D
B
C

B
C
C
b
a
B
C
0
c
6
D
A
C
B
C
B
A


C
C

c
0
c
B
C
B
0
D
B
B
C
2
2
2
2
2
2
2
2
2
1
2
3
3
2
3
3
2
1
3
2
3
2
2
2
3
2
2
2
2
2
2
2
1
2
3
2
2
3
3
1
3
2
3
2
3
3
3
2
2
3
3
3
3
2
3
2
3
2
3
2
2
3
3
3
3
I
2
3
2
3
3
3
3
S
2
3
2
                                                 25

-------
        Table  3  (continued).    PRIORITIZATION  LISTING  -

                                INORGANIC  SOURCES

SODIUM SILICATES                                                             9,000       2
POTASSIUM PERMANGANATE AND MANGANESE DIOXIDE                                   9,000   C    3
FERTILIZER MIXING  -  AMMONIATION - GRANULATION PLANTS                           7,000   6    2
CHROMIUM OXIDE  - INORGANIC PIGMENT                                            7,000   C    3
ANTIMONY OXIDE                                                                7,000   0    3
ZINC CHROMATE - PIGMENT                                                       7,000   0    3
BARIUM SULFATE  - PIGMENT                                                      6,000   C    3
CALCIUM PHOSPHATE                                                             6,000       3
SODIUM SULFIDE                                                                6,000   C    3
TIN COMPOUNDS - HALIDES, OXIDES, SULFATCS.  OTHERS                              6,000   C    3
POTASH - POTASSIUM SALTS                                                      s.ooo   c    3
ARSENIC TRIOXIDE                                                             S.OOO   0    3
FERTILIZER MIXING  -  LI8UIO MIX PLANTS                                         5,000   8    2
ALUMINUM HYDROXIDE-                                                           5.000   C    2
HYDROCHLORIC ACIU                                                             5.000   8    2
PERLITE MANUFACTURING                                                         If.OCO   C    2
ABRASIVE PRODUCTS                                                             "4.000   C    2
SODIUM FLUORIDE                                                              *,ooo   c    3
HYDRAZINE                                                                    <»,000   C    3
BARIUM CARBONATE                                                             3.000   C    3
HYDROGEN CYANIDE                                                             3,000   B    3
CALCIUM CARBONATE                                                             3.000   C    3
SODIUM SULFAU  - NATURAL PROCESS ONLT                                         2,000   C    3
ALUMINUM SULFSTE                                                             2,000   C    2
SODIUM ARSENITE                                                              2,000   0    2
EXFOLIATED VLRMIcULlTE                                                        2.000   C    2
SODIUM HYDROSULFIDE  - SODIUM BISULFIDE OR  SULFHYDRATE                          1.000   C    3
NICKEL COMPOUMIS - EXCEPT NICKEL SULFATE                                      l.OCO   C    2
ALUMINUM CHLORIDE  -  ANHYDROUS                                                 1.000   C    2
MAGNESIUM COMPOUNDS  - CARBONATE, CHLORIDE,  OXIDE S HYDROXIDE                   1.000   C    2
SODIUM THIOSULFATE - SODIUM HYPOSULFITE                                        1,000   C    3
SODIUM SULFITE                                                                  600   C    3
IHON CHLOKIDE • FFRRIC                                                          soo   c    2
SODIUI* CHLORATE.                                                                700   C    3
«CRYLLIUM CO«f"JUfgDS                                                             bOO   D    *
CALCIUM ARSE.NATE                                                               "»00   0    3
                                                                               "»00   C    ?
       HYDROSULFITL                                                             ^00   C    3
SODIU* CARBONATE - NATURAL                                                      HOO   C    3
CONVERSION OF CRUDE  IODINE TO RESUBLIMED AND IODINE PRODUCTS                     300   C    2
POTASSIUM SULFATE                                                               300   C    3
MISCELLANEOUS SODIUM COMPOUNDS                                                  100   C    2
CHROMIUM COMPOUNDS - ACETATE, BORIDES. HALIDLS. ETC.                             100   D    2
SODIUM NITRITE.                                                                   70   C    3
SULFUR MONOCHLORIDE  AND DICHLORIDE                                               50   C    3
LITHIUM SALTS - LITHIUP CARBONATE AND LITHIUM HYDROXIDE                            7   C    3
CRUDE IODINE  -  DOMESTIC PRODUCTION                                                6   C    3
PHOSPHORUS OXYCHLORIDE                                                            2   C    3
SECONDARY MAGMLSIUM  SMELTING                                                      2   C    2
                                            26

-------
      Table  4.    PRIORITIZATION  LISTING  -  ORGANIC  SOURCES
                                  ORGANIC SOURCES
          SOURCE TYPE

SOLVENT EVAPORATION - DECREASING
FAdRIC SCOUR INb
PETROLEUM REFINING - FUGITIVE  EMISSIONS
THICHLOROETHYLENE - FROM  ETHYLENE
PETROLEUM REFINING - WASTE  WATER PLANT
PETROLEUM EXTRACTION
NATURAL GAS DISTRIBUTION
GASOLINE DISTRIBUTION - AUTOMOBILE TANK LOADING
SURFACE COATING . SHEET,  STRIP AND COIL COATING
PETROLEUM REFINING - BLENDING  AND STORAGE
SURFACE COATING . PAPER AND PAPERBOARD COATING
POLYVINYL CHLORIDE
NATURAL GAS EXTRACTION
SOLVENT EVAPORATION - RUBBER AND PLASTIC PROCESSING
SOLVENT EVAPOOATION - ORYCLEANING
SURFACE COATING - FABRIC  TREATMENT
SOLVENT EVAPORATION - PRINTING AND PUBLISHING
ASHHALT PAVING - HOT MIX
SOLVENT EVAPORATION - SURFACE  COATING - AUTO PAINTING
ASPHALT ROOFING
PETROLEUM REFINING - CATALYTIC CRACKING
SURFACE COATING - MAJOR APPLIANCE FINISHING
EThYLEME OICHLORIDE - OXYCHLORINATION
EThYLEHE OICHLORIDE - ETHYLENE CHLORlNATION
VARNISH MANUFACTURERS
PHTH4LIC ANHYDRIDE - 0-XYLENE
GASOLINE DISTRIBUTION - SERVICE STATION TANKS
EThYLE'JE-PROPYLENE RUBBER
ACRYLIC ACID
AKTIFICIAL RIPENING OF FRUITS  AND VEGETABLES
DEEP FRYING
NSOPRENE
MALT BEVERAGE  PRODUCTION
PETROLEUM REFINING - VACUUM DISTILLATION
FRUIT AND VEGETABLE CANNING
VINYL CHLORIDE - ETHYLENE DICHLORIDE
ETHYL CHLORIDE
SURFACE COATING - INDUSTRIAL MACHINERY FINISHING
TRICHLOROETHYLEfE - FROM  ACETYLENE
SURFACE COATING - METAL FURNITURE FINISHING
PETROLEUM REFINING - SULFUR PLANT
f-ETROLEUM REFINING • ASPHALT PLANT
PRINTINP INK
2-i.THYL-l-HEXANOL
UIMETHYL TEREPHTHALATE
SURFACE COATING - WOOD FURNITURE FINISHING
ACETONE - FROf CUMENE
WOOD PROCESSING - KRAFT OR  SULFATE PROCESS
SURFACE COATING - SMALL APPLIANCE FINISHING
PERCHLOROETHYLENE - CHLORlNATION Of PROPANE
CAhHON TETRACHLORIDE - CHLORlNATION OF PROPANE
POLYFTHYLENE RESIN - HI&H DENSITY
PtTROLEU" REFINING - CRUDE  OISlILLATICN
POLYSTYRENE RESH.
CRESOL - SYNTHETIC
POLYETHYLENE RESIN - LOW  DENSITY
POLYHETHYLENE POLYPHENYL  ISOCYANATE
CARBON BLACK • FuRNACE
FRUIT AND VEGETABLE FREEZING
METHYL METHACRYLATE
CYCLOHEXANONE
ASPHALT PAVING - DRYER DRUM PROCESS
ADIPONITRILE
METHYL IS09UTYL KETONE
ACETIC ANHYDRIDE
PLYWOOD AND VENEER DRYING
PHENYLKERCURY OLEATE
PHENOL - CUMENE PROCESS
FORMALDEHYDE
GLYCERIN TRIPOLYOXYPROPYLENE ETHER
ACRYLONITRILE
MALE1C ANHYDRIDE FROM BENZENE
PHTHALIC ANHYDRIDE - NAPHTHALENE
GASOLINE DISTRIBUTION - TERMINAL LOADING AND STORAGE
i/INYL ACETATE - FROM ETHYLENE
FUMARIC ACID
                                                                     IMPACT  FACTOR
                                                                                     UL  CALC
100, 000, (100,000
1,000,000,000
JOO.000,000
200,000,000
60,000,000
50.000,000
30,000,000
20,000,000
20,000,000
10,000,000
10,000,000
10,000,000
10,000,000
a. ooo, ooo
7,000,000
6,000,000
3,000,000
3,000,000
1,000,000
1,000,000
POO, 000
700,000
700,000
700,000
600.000
UOO.OOO
300,000
300,000
300,000
300,000
300,000
300,000
300,000
200,000
200,000
200.000
200,000
200,000
200,000
200,000
200,000
200,000
200.000
200,000
200,000
100,000
100,000
100,000
IOC, 000
100.000
100.000
100,000
100, OCO
100.000
100.000
100,000.
100.000
90.000
80,000
BO, 000
70,000
70.000
60,000
60,000
60.000
60,000
30,000
30,000
SO. 000
50,000
to, ooo
to, ooo
HO, 000
HO, 000
30,000
30,000
B
D
c
B
c
B
B
A
c
c
c
A
B
C
c
c
c
B
C
C
B
C
B
B
0
B
A
C
B
D
D
A
C
B
C
B
B
C
B
C
B
B
D
B
C
C
C
9
C
B
8
B
R
C
B
B
C
B
C
B
B
0
C
C
B
C
0
B
C
C
B
B
B
A
B
C
1
2
2
3
2
2
2
1
Z
2
2
2
2
2
1
2
1
1
2
1
2
2
3
3
2
3
1
3
3
1
1
3
2
2
?
3
3
2
I
2
2
2
2
3
3
2
3
2
2
3
3
3
2
2
3
3
3
2
2
3
3
1
3
3
3
2
3
3
2
3
3
3
3
1
3
3
                                            27

-------
      Table  4   (continued).    PRIORITIZATION  LISTING  -

                                ORGANIC  SOURCES


 SURFACE COATINS - FARM MACHINERY  FINISHING                                    30,000   C   2
 SURFACE COATINS - COMMERCIAL MACHINERY FINISHING                              30.000   C   2
 VINYL CHLORIDE . ACETYLENE                                                   30,000   8   3
 GLYCERIN - ALLYL ALCOHOL                                                     30,000   C   3
 NATURAL GAS PROCESSING                                                       30,000   a   2
 PAJNT MANUFACTURING                                                          20,000   0   2
 POLYESTER RESINS - UNSATURATEO                                                20,000   C   2
 HOOD PROCESSING . SULFITE PROCESS                                             20.000   8   2
 OICHLORODIFLUOROMETHANE                                *•                      20.000   C   3
 HEXAMETHYLENE.1ETRAMINE                                                       20.000   C   3
 KELTHANE                                                                     10,000   D   3
 GLYCERIN . ACHOLEIN                                                          10,000   C   3
 METHANOL                                                                     10,000   C   3
 COTTONSEED OIL MILLING                                                       10.000   C   2
 SOAP AND OETERGFNTS                                                          10,000   C   2
 POLYCHLORINATLO 8IPHENYLS                                                    10.000   C   3
 CARBON TETRACHLORIDE • METHANE                                                10.000   8   3
 AKINO RESINS                                                                 10,000   c   2
 SUGAR PROCESSING                                                             10.000   0   2
 ACETIC ACID                                                                   9.000   B   3
 0-XYLE.NE                                                                      6,000   C   3
 P-XTLENE                                                                      8.000   8   2
 PETROLEUM REFINING - FLARES                                                    6.000   B   2
 NTLON kt                                                           '           6.000   B   2
 D01ECYLBENZENE SULFONIC ACID -  SODIUM SALT                                     6.000   C   2
 VEGETABLE OIL MILLING                                                         6.000   C   2
 GLYCERIN - ALLYL CHLORIDE                                                     7,000   C   3
 N-BUTYL ALCOHOL                                                               7.000   C   3
 COFFEE ROASTING                                                               7,000   B   2
 MALATHION                                                                     7.000   D   3
 METHYL PAKATM10N                                                              6.000   C   3
 ACETALDEHYOE - OXIDATION OF  ETHANOL                                            6.000   C   3
 WOOD PROCESSING - NEUTRAL SULFITE  SEMI-CHEMICAL                                6.000   B   2
 POLYVINYLVINYLIDENE CHLORIDE                                                  5,000   D   3
 LEATHER                                                                       5,000   0   1
 AOIPIC ACID                                                                   5,000   B   3
 PETROLEUM REFINING - ETHYLENE I»L*NT                                            5,000   C   2
 CUMENE                                                                        5.000   C   2
 STYRENE                                                                       H.OOO   B   3
 CHLOROSULFONIC ACID                                                           4,000   C   3
 DOOECYLBENZENE - HARD                                                         4.000   C   3
 DOT                                                                           4,000   C   3
 PtNTAERYTHRITOL      .                                                         4,000   C   3
 ISOCYANATES                                                                   4.000   B   3
 POLYACRYLONITRILE - POLYMERIZATION SOLUTION                                    4,000   C   3
 CYCLOHEXANE                                                                   4,000   C   3
 ACETYLLNE                                                                     1,000   C   3
 EPICHLOROHYDRIH                                                           •    4,000   8   3
 UET CORN MILLING                                                              4,000   D   2
 OODECYLBENZENE SULFONIC ACID                                                  4,000   C   2
 ACETONE CYANOHYDRIN                                                           3,000   C   3
 POLYURETHANE ELASTOMER                                                        3.000   C   2
 ACETIC ACID - FROM METHANOL                                                    3,000   C   3
 METHYLENE CHLORIDE - CHLORINATIQN  OF BETHANE                                   3,000   B   3
 ACETYL CHLORIDE                                                               3,000   D   3
 POLYURETHANE SURFACE COATING RESINS                                            3.000   D   2
 CRESYLIC ACID                                                                 3,000   B   2
 PETROLEUM REFINING - CATALYTIC  REFORMING                                       3.000   B   2
 NYLON 6                                                                       3.0CO   B   2
 MIXED OLEFINIC PRODUCT                                                        3,000   C   3
 MIXED LINEAR ALCOHOL                                                          3,000   C   2
 PETROLEUM REFINING - CATALYTIC  HYDROREFINING (HOS)                              3,000   B   2
 UREA                                                                          3,000   C   2
 FORMIC ACID                                                                   3.000   C   3
 LINEAR ALKYLBENZENE                                                           3.000   C   3
 HEPTACHLOR                                                                    3.000   C   3
 ENORIN                                                                        3.000   D   3
 WASTE SOLVENT PROCESSING                                                      2.000   0   1
 NONYLPHENOL                                                                   2.000   C   3
OODECYLRENZENE SULFONIC ACID •  CALCIUn SALT                                    2.000   C   3
 MEAT SMOKEHOUSES                                                              2,000   D   2
 DISTILLED LIQUOR                                                              2,000   C   1
 TOLUENE DIISOCYANATE                                                          2.000   C   3
 TEREPHTHALIC ACID                                                             2.000   B   3
0-UICHLOROBENZLNE                                                             2.000   B   3
HYOROOUINONE                                                                  2,000   C   3
CARBON TCTRACHLORIDE - CARBON OISULFIDE                                        2.000   B   3
 ISOPRENE - 2-METHYL-1.3-BUTAOIENE                                              2.000   C   3
HEPTENE                                                                       2,0.00   C   3
DI-2-ETHYLHEXYL PHTHALATE                                                    '  2.000   C   2
ETHYLENE DIBROMIDE                                                             2,000   C   3
                                         28

-------
         Table  4   (continued).    PRIORITIZATION  LISTING  -
                                   ORGANIC  SOURCES
NITROBENZENE
NAPHTHALENE - COAL TAR
N-PARAFFIN CHLORIDE
ENOOSULFAfi - THIOOAN
PROPYLENE OXIDE - CHLOROHYORIN PROCESS
ALKYD RESINS
PCLYAMIDE RESINS
ETMYLENE OXIDE
CELLULOSE ACETATE
POLYURETHANE FIBERS
ALDFIN
iPOXY RESINS - UNMODIFIED
S-3UTYL ALCOHOL
RAYON - SEMI SYNTHETIC VISCOSE RAYON
TOLUENE SULFONATE - HYOROTROPE
LTHYLENE - PROPYLENE TERPOLYMEK
ISOPHTHALIC ACID
OXALIC ACID
lil.l-TRICHLOROETHANt
FOOD PREPARATION
0X0 PROCESS
BENZYL CHLORIDE
CARBON OISULFIOE
CHLOROACETIC  ACID
SORBITOL
OIISOOECYL PHTHALATE
AMMONIUM QXALATE
CHLOROPHENOL
CHLOROFORM
0X0 MIXED LINEAR  ALCOHOLS
KETONE ALCOHOL .OIL
DECYL ALCOHOL
BISPHENOL-A
ACETALOEHTOE  -  HYORATION OF ETHYLENE
ASCORBIC  ACID  -  VITAMIN C
POLYESTER  POLYOLS
METHYL CHLORIDE
P-DICHLOR08ENZENE
METHYL ETHYL  KETONE
POLYVINYL  ALCOHOL RESINS
SALICYLIC  ACID
N-OCTYL-N-OECYL  PHTHALATE
POLYPROPYLENE
CHLOROBENZENE
ANTHELMINTICS
OIISOOCTAL PHTHALATE
HEXAMETHYLENEOIAMINE  -  ADIPONITRILE
SULFATfO FTHOXYLATES  -  AEOS
TPIMETHYLANINL
CAKBARYL-SEVIN
PARAFORMALOEHYDE
LINDANE
TETRACYCLINE
GLYCERIN - EPICHLOHOHYORIN
ANILINE
VINYL ACETATE - FROM  ACETYLENE
FISH AND SEAFOOD  CANNING
POLYVINYL ACETATE RESINS
Z.t-U - DIMETHYLAMINE SALT
MONOETHYLAMINE
ETHAMOL
TKlETHYLfll"IINE
SYM-TRIMETHYLtNE-TRINITPAMINE
SACCHARIN
DODECYLBENZENE SULFONIC ACID - ISOPROpYLENINE  SALT
ASPIRIN
"OOACRYLIC FIBERS
DIETHYLAMINE
ETHANOLAP1NE - MONO-. DI-. AND TRI
PYRETHRINS
ACETONE - FROM ISOPROPANOL
POLYRA1
TFICHLOROTRIFLUOROETHANE
DOOECYLBENZENE SULFONIC ACID - TRIETHYLAMINE SALT
M-XYLENE
2.
-------
            Table  4   (continued).    PRIORITIZATION LISTING  -

                                     ORGANIC  SOURCES



 ISOOCTAL ALCOHOLS                                                               200   C   3
 2t
-------
            Table  4   (continued).    PRIORITIZATION  LISTING

                                      ORGANIC  SOURCES
VINYL BROMIDE
ETHYL ETHER
TOLUENE-2.  <»-UIAMINE
ACROLEIN
POLYISOPRENE
PkOPYLENE TRIMER
N-HUTYRALOEHYOE
PYROGALLIC  AGIO
CATECHOL
BUTYLENE OIMEN - OIISOBUTYLENE
AMMONIUM TARTRATE
OIQUAT
POLYCARBONATE RESINS
POLYISOBUTYLENE - ISOPRENE BUTYL
DOOECENE -  NON-LINEAR
HETHANEARSONIC ACID - NONOSODIUM SALT  - MMA
ETHOXTLATED OcTYLPHENOL
ETHOXYETHANOL
CYCLOHEXYLAMINE
XYLENE SULFONATE - SODIUM SALT
S-BUTOXYETHANOL
2.t.5-I
BEN2EHE
MEVINPHOS
METHANEARSONIC ACIO - CALCIUM SALT  . CALAR
ALLYL ALCOHOL
PETROLEUM REFINING - AROMATICS/ISOMERIZ»TION
PtNICILLIN  G - PROCA1NE
OICHLOROBENZONITRILE
PHENYIHERCURY ACETATE - PMA . PMAS
ETHYL BENZENE
PROPIOMC ACIO
DI-SYSTON
ETHYL PYROPHOSPHATE - TEPP
ETHOXYLATED MUED LINEAR ALCOHOLS
OALAPON
PETROLEUM REFHUNG - ALKYLATION
CUMENE SULFONATE - AMMONIUM SALT
DI BUTYL PHTHALATE
UUHSBAN
CUMENE SULFONIC ACIO
TOLUENE SULFONIC ACID
DIUTROBENZENL
1.5-CYCLOOCTADIENE
ALCOHOL SULFATE - SODIUM SALT
ISOPROPYL ACETATE
AMMONIUM BENZOATE
CAPTAN
AMMONIUM THIOCYANATE
CINITROPHENOL
XYLENE SJLFOUATE - AMMONIUM SALT
ALCOHOL SULFATES - TklETHANOLAMINE  SALT
lilTHOGLYCLRINE
ALCOHOL SULFATES - AMMONIUM SALT
2-ETHOXYETHYL ACETATE
BINZONITRILE
CHOTO^ALDEHYDE
METHYL ACETATE
AKYL ACETATE
LINEAK ALCOHOLS - ZIEGLER PROCESS
T-8UTYL ALCOHOL
NlTROPARiFINS
HYDROXYLAMINE
XYLENE SULFONATF - POTASSIUM SALT
LI-2-ETHYLHEXYL AOIPATE
URUCINE ALKALOID
ALLYL CHLORIDE
OLEIC ACID
GUTHION
N-BUTYRIC ACID
ETHYL BUTTRATE
CARBON BLACK - THERMAL
STYHENE - BUTADIENE COPOLYMER RESINS
DIMETHYL HYORAZINE
HYDROXYLAMINE SULFATE
10
10
10
10
10
10
10
10
10
10 '
9
9
9
9
9
6
7
7
7
7
6
6
3
5
5
5
5
S
S
3
n
<*
u
It
n
14
3
i
i
3
2
2
2
2
2
2
2
2
2
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
0
C
a
B
c
c
c
0
0
c
0
0
B
C
c
c
0
c
c
c
c
0
c
0
c
0
B
c
0
0
c
c
c
0
c
0
c
D
c
0
0
D
D
C
C
C
c
D
0
D
C
C
C
C
D
D
D
C
D
C
C
B
0
C
C
D
B
C
C
D
C
A
B
D
D
3
3
2
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
2
3
3
3
2
3
3
3
2
3
3
3
2
3
2
3
2
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
2
3
3
2
3
3
3
3
2
3
3
                                                31

-------
            Table  5.    PRIORITIZATION LISTING  - OPEN SOURCES
                                      OPEN SOURCES
           SOUHCE  TYPE

 FIELD FOP*ULATIOfc OF PESTICIDES
 UNHAVED ROADS
 AGRICULTURAL TILLING
 CONSTRUCTION ACTIVITIES
 WIND EROSION UF SOIL FROM DORMANT LAND
 HLASTING OF  SULFUR STORAGE PILES
 PARAThlON APPLICATION ON CROPS
 CRUSHED GRANITE
 TOXAPHENE APPLICATION ON CHOPS
 CRUSHES SANDSTONE
 HANDLING OF  GRAIN
 C01T1N HARVESTING
 CRUSHED LIMESTONE
 TRANSPORT OF SAND ANO GRAVEL
 OPEN MINING  OF COAL
 COAL ASH DISPOSAL
 LOADING OF SAND AND GRAVEL
 GRAIN HARVESTING
 UAKITE MILLINf-
 ABPASIVE CLEANING OF OUTDOOR STRUCTURES
 CRUSHED STONE/TRAPROCK
 DEFOLIATION  Of COTTON
 INDUSTRIAL SAMD HANDLING
 COAL FINES DISPOSAL
 PAPER HILL BUILDING EMISSIONS
 CRUSHINGt SIZIHG  OF SAND ANO GRAVEL
 OPEN STORAGE PF SAND AND GRAVEL
 CHLOR1NATION OF SHIMMING POOLS
 STORAGE OF ANIMAL  RENDERINGS
 POULTRT DRESSING
 SIZING. GRINDING,  FIBERIZING OF ASBESTOS
 SAND AND GRAVEL UNLOADING
 BUILDING DEMOLITION
 HANDLING OF  CONCRETE PRODUCTS
 SCREENING. CRUSHING OF CLAT
 H V TRANSMISSION  LINES
 COAL TRANSPORT
 DISPOSAL OF  AbBESTOS WASTE ORE
 BEEF CATTLE  FEEDLOTS
 CONVEYING OF SAND  AND GRAVEL
 MINING ANO BLASTING OF ASBESTOS ORE
 PHOSPHATE ROCK OPEN STORAGE
 PHOSPHATE ROCK LOADING
 REFUSE ASH DISPOSAL
• SEWERAGE CHLORINATION TANKS
 LOADING HEADY-MIX  CEMENT
 STORAGE OF WOOD CHIPS
 CLAY PROCESSING AREA
 REFUSE UNLOADING
 LOADING HfORAULIC  CEMENT
 DISPOSAL OF  CONCRETE BLOCK WASTES
 STORAGE OF ASHESTOS ORE
 TRANSPORT OF ASBESTOS ORE
 TRANSPORT OF CLAY
IMPACT  FACTOR
                UL  CALC
2.000. 000. 000.000
800,000,000.000
300.000.000.000
100.000.000.000
70.000.000.000
6. 000*000.000
3.000,000.000
3.000.000,000
2.000.000.000
2>000,000.000
2.000,000,000
2.000,000,000
1.000.000,000
900,000.009
500,000.000
400.000.000
000
30,000.000
20.000,000
20<000(000
20(000(000
10(000(000
10.00U.OOO
10,000,000
10,000,000
10,000(000
10(000,000
9,000,000
7,000,000
7,000,000
6,000,000
6,000.000
0,000,000
4,000,000
4,000,000
3,000,000
2,000.000
?. 000. 000
900,000

c
c
c
c
c
c
c
c
c
0
B
c
c
c
c
c
B
B
D
c
B
B
c
D
c
B
c
D
0
B
c
D
0
c
c
0
c
B
c
B
A
A
0
c
B
D
A
D
8
0
B
B
n
s
4
2
1
2
2
2
1
2
1
1
2
1
2
2
1
2
2
2
1
1
2
?
2
?
2
2
1
1
1
2
2
1
1
2
1
4
2
2
2
2
2
?
1
1
2
2
2
1
2
1
2
2
2
                                               32

-------
   Table  5   (continued).    PRIORITIZATION LISTING  -
                             OPEN  SOURCES
SlOHAGf OP SAUUUST                                                        800,000   0   2
COAL  CONVEYING                                                           800,000   0   1
ALKALI ANO CHLORINE PLANT WASTES                                           700,000   C   2
LOADING LIME                                                             600,000   C   2
SEWERAGE TRICKLING FILTER                                                 500,000   C   1
SAW MILL WASTE STORAGE                                                    500,000   C   2
COAL  STORAGE                                                             300,000   A   2
LJhILLING OIL AND GAS - BEFORE WELL HIT                                     200,000   B   2
OPEN  MINING OF TALC                                                       200.000   C   2
ASBESTOS PROCESSING AREA                                                  100,000   D   2
TRANSPORT OF SULFUR                                                       iou,ooo   c   2
LOADING OF FINISHED CLAY                             .                      90,000   P   2
STORAGE OF RAW CLAY                                                        90,000   D   2
CLAY  SILOS - KAOLIN                                                        70,000   A   2
SfWERAGE AERATION                                                         60,000   C   1
STORAGE OF SULFUR                                                         60,000   C   2
OPEN  MINING AND GRINDING OF PUMICE                                          50,000   C   2
TKANSPORT OF TALC ORE                                                      50,000   C   2
STORAGE OF TALC ORE                                                        »0,000   c   2
SEWtRAGE VACCUUK FILTER                                                    30,000   C   1
BARITE STORAGL                                                            30,000   8   2
BARITE TRANSPORT                                                          20,000   8   2
OPEN  MINING ANU STORAGE OF MICA                                             20,000   c   2
OPEN  CLAY MINING                                                          20,000   0   2
                                       33

-------
                   SECTION III




                   APPENDIXES






 DETAILED EXAMPLES USING PRIORITIZATION MODEL






A.  Use of Model with Common Inputs




B.  Example of Population Sensitive Calculation




C.  Location Sensitive Calculations




D.  Example of Detailed Calculation




E.  Example of Open Sources Calculation
                       35

-------
                        APPENDIX A

              USE OF MODEL WITH COMMON IMPUTS
Since published standards exist for the five criteria

pollutants, it was deemed inappropriate to use TLVs for

these materials.  Instead, the primary standard, S, was

set equal to the hazard potential factor, F.   Common
constants used were:.
               u = wind speed = 4.5 m/sec

               e = 2.72

               TT = 3.14
aln the organic materials category, emissions that were
 specifically identified as organic were termed  "named
 hydrocarbons" to differentiate them from the criteria
 hydrocarbon emissions of indeterminate composition.  The
 hazard potential factor for these materials was defined
 as follows:

              (TLV.K if TLV.K < S0-
          F = I                  HC
              (  SHC if TLV.K > SHC


where  SHC = hydrocarbon standard = 0.16 mg/m3


and      K =  (40/168)(1/100)


                             36

-------
Table A-l gives the population and area data for the 50
states.1*  Table A-2 lists the ambient air quality for the
criteria pollutants.5
uThe World Almanac and Book of Facts, 1974.

5Air Quality Data - 1972 Annual Statistics.  Publication
 No. EPA-450/2-74-001.

                            37

-------
        Table A-l.   POPULATION AND AREA DATA BY STATE


1
2
3
4
b
6
7
H
~f
10
11
12
13
14
15
16
17
18
I')
20
21
22
*3
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
so
STATf

ALABAMA
ALASKA
ARIZONA
ARKANSAS
CALIFORNIA
COLOKAUQ
CONNECTICUT
UELAWARE
FLORIDA
uEOKOIA
HAWAII
IDAHO
ILLINOIS
INDIANA
IOWA
KANSAS
KENTUCKY
LOUISIANA
MAINE
MARYLAND
MASSACHUSLTTi
MICHIGAN
MINNESOTA
MISSISSIPPI
MISSOURI
MONTANA
NEBRASKA
NEVADA
NEW HAMPirtlHt
NEW JERSEY
NEW MEXICO
NEW YORK
N CAHOLINA
N DAKOTu
OHIO
OKLAHOMA
OREGON
PENNSYLVANIA
RHODE ISL'M
S CAROLINA
S DAKOTA
TENNESSEE
TEXAS
UTAH
VERMONT
VIRGINIA
WASHINGTON
W VIRGINIA
WISCONSIN
WYOMING
POPULATION

3521000.
325000.
1963000.
20U80UO.
2U411000.
2364000.
3080000.
571000.
7347000.
4733000.
816000.
7550UO.
11244000.
5286000.
2684000.
2268000.
3306000.
3738000.
1026000.
4800000,
5796000.
9013000.
36770UO.
2256000.
4747000.
716000.
1523000.
533000.
774000.
7349000.
1076000.
18367000.
5221000.
634000.
10722000.
2633COO.
2185000.
11905000.
969000.
2668000.
680000.
40720UO.
11604000.
1127000.
4600UO.
4765000.
3418000.
1795000.
4526000.
346000.
POPULATION
FRACTION
0.0169U93
0.0015608
0.0094272
O.OU96433
0.0980223
0.0113529
0.0147915
O.OU27422
0.0352834
0.0227299
0.0039186
0.0036256
0.0539985
0.0253856
0.0136502
U. 0108919
0.0158768
0.0179515
0.0049273
0.0230516
0.0276349
0.0432843
0.0186190
0.0108343
0.0227971
0.0034385
0.0073381
0.0025597
0,0037171
0.0352930
0.0051674
0.0882062
0.0250735
0.0030447
0.0514916 .
0.0126448
0.0104933
0.0571729
0.0046536
0.0129069
0.0032657
0.0195555
0.0557274
0.0054123
0.0022091
0.0228836
0.0164147
0.0086204
0.0217358
0.0016616
AREA

51609.
586412.
113909.
53104.
158693.
104247.
5009.
2057.
58560.
58876.
6450.
83557.
56400.
36291.
56290.
82264.
40395.
48523.
33215.
10577.
8257.
58216.
84068.
47716.
69666.
147138.
77227.
110540.
9304,
7836.
121666.
49576.
52586.
70665.
41222.
69919.
96981.
45333.
1214.
31055.
77047.
42244.
267338.
84916.
9609.
40817.
68192.
24181.
56154.
97914.
AREA
FRACTION
0.01428
0.16221
0.03151
0.01469
0.04390
0.02884
0.00139
0.00057
0.01620
0.01629
0.00178
0.02311
0.0156'!
0.01004
0.01557
0.02276
0.01117
0.01342
0.00919
0.00293
0.00226
0.01610
0.02325
0.01320
0.01926
0.04070
0.02136
0.03058
0.00257
0.00217
0.03366
0.01371
0.01455
0.01955
0.01140
0.01934
0.02683
0.01254
0.00034
0.00859
0.02131
0.01169
0.07395
0.02349
0.00266
0.01129
0.01886
0.00669
0,01553
0.02709
NO OF (
COUNTIES
67.
29.
14.
75.
58.
63.
8.
3.
67.
159.
5.
44.
102.
92.
99.
105.
120.
64.
16.
23.
14.
83.
87.
62.
114.
56.
93.
16.
10.
21.
32.
62.
100.
53.
88.
77.
36.
67.
5.
46.
67.
95.
254.
29.
14.
96.
39.
55.
72.
23.
'OPULATW
UENSHV
66.223
0.554
17.233
37.S13
128.619
22.677
614.893
277. Sli*
125.461
80.389
126.512
9.U36
199.362
145.656
51.* 13
27.570
61.842
77.U36
30.89U
453.815
701. 95U
154.820
46.117
47.28U
66.12U
4.866
19.7B6
4.822
83.190
937. 8S1
8.844
370.482
99.285
*. 972
260. 1U4
37.658
22.530
26'. 612
798.188
«6.bb6
£ . 026
96.392
43.406
13.272
47.H72
116.741
50.123
74.232
80.6UU
3.534
TOTALS
             208228064.
                       l.OOOU
                             3615055.
                                     1.0000
Legend
     Area  is  given in square  miles.
     Population density  is  given in persons/mi2
                              33

-------
            Table  A-2.   AMBIENT AIR QUALITY  DATA BY STATE
                        FOR CRITERIA POLLUTANTS
STATE     PANTICULATES
  1    63   0.22366003
  2    111   0.34200E-03
  i    32   0.31672E-OJ
  4    32   0.14731E-03
  5    19   0.21937E-03
  6    69   0.28899E-03
  7    26   0.1838SE-03
  h    16   C.17169E-03
  <»    43   0.12393E-03
  10    31   Q.1.19451-03
  11    m   0.14300E-03
  12    30   0.2f.080L-03
  13    ft   U.11204E-03
  14    128   U.20084E-03
  IS    3U   0.21S10E-03
  1(>    39   0.19697E-03
  17    90   D.17910E-03
  IS    12   0.17267E-03
  19     7   0.83000E-04
  21.    85   0.15182E-03
  21    52   C.15679E-03
  ?V    109   0.20440E-03
  ?5    59   0.14237E-03
  ?4     2   0.93000E-04
  «!5    49   0.20S90E-03
  ?o     2   0.92000E-04
  27    36   0.16975E-03
  2h    "41   0.371001-03
  2V    26   0.14292E-03
  3li    79   0.13514L-03
  31    28   0.248UOS.-03
  32    233   0.1-J260E-03
  .53    199   0.1B053(-03
  34    16   0.2223fl£-03
  35    137   0.27228E-03
  .16    9b   G.19453E-03
  37    48   0.16067E-03
  Jo    105   0.24043E-03
  39    23   0.14004E-03
  40    75   0.20008E-03
  41     2   0.13650L-03
  42    96   0.1H928E-03
  43    192   0.231UBL-03
  44    • 8   0.43513L-03
  45     2   0.16000L-03
  4fr    122   0.198UOL-03
  47    57   O.P.1718E-03
  4(i    38   0.20964E.-03
  4'j     7   0.14586E-03
  50     4   0.95750E-04
CAKBOM HONOXIOL
2
1
2
0
51
1
0
0
6
?
1
0
1
3
2
5
7
3
0
19
3
3
3
0
10
0
1
1
0
22
1
13
2
0
12
3
2
2
2
0
1
4
1
4
0
9
10
1
1
0
0.15200E-01
0.46UOOE-01
C.552UOC-01
0.4UUOOE-01
0.21300E-U1
0.494UOE-01
C.HOUOOE-01
0.4UUOOE-01
0.23900C-01
0.23UOOE-01
0.37HOOE-01
U.40000E-01
0.27faUOC-Ul
0.12100E-01
0.13200E-01
U.26200E-01
0.27^00E-01
O.ltt^OOE-01
U.40UOOE-01
U.19ZOOE-01
0.326UOC-01
0.1304
O.B6700E-04
U.95500F-0»>
0.43700E-04
0.79700E-04
C.11640E-03
0.95SOOE-04
0.11730E-03
0.26000E-04
0.73500E-04
0.13000E-U4
0.11720E-03
0.46270E-03
0.10750F-03
0.73200E-04
0.25200E-04
0.13360C-03
0.69900E-04
0.80000E-04
0.14450E-03
0.794UOE-04
0.99000£'04
0.71300C-04
0.14780E-03
U.44100E-04
0.70000E-05
0.29000E-04
0.26100E-04
0.50000E-04
U.80000E-04
0.79300E-04
0.52800E-04
0.11630E-03
0.61300E-04
0.13SOOE-04
NITGN UIOXIUE
13
I
5
?
14
2
4
3
22
13
11
n
4
40
2
29
3^
4
1
38
42
6
3
2
4
1
3
0
4
8
7
8
72
n
30
19
1
14
15
16
1
23
13
A
0
6
10
1
3
2
0.71400C-04
0.96500F-04
0.h69COL-04
n. (\03onr.-04
0.1762'.lL-n3
0.8630nE-04
0.15340E-03
0.88700E-04
n.ii76nE-n3
0.42iur>r.04
0.4370'JF-04
0.100001-0}
O.ltlilOC-0'5
n.i0740E-ns
0.84000E-04
5.3270CE-04
o.tieonr-oi.
0.105brl-03
o.35ounr-ou
0.71500L-04
0.770COE-C4.
n,13?7nE-n3
0.9b30PE-04
0.61800E-04
0.92300E-04
0.240COE-04
0.65SOOE-04
0.10000E-03
0.25600E-04
0.10980E-03
0.497UOE-04
0.10540E-03
0.450UGE:-04
U.10000E-OS
0.146tOE-03
0.51900E-04
0.12SOOE-03
0.10190E-OJ
0.84000E-04
0.47800E-04
0.38000E-04
0.51000E-04
0.94100E-04
0.1S9COE-t!J
0.10000E-03
0.863UOE-04
0.86800E-04
0.11500E-0?
0.77200E-04
0.28500E-01*
HYDROCARBONS
2
0
2
0
37
1
0
U
1
'1
0
0
1
0
0
0
7
U
0
12
0
b
2
0
9
U
0
1
0
4
0
10
1
0
2
U
1
1
0
0
U
0
0
c
0
1
3
0
U
0
0.10839E-01
o.noooOE*oo
U.48880E-02
o.onoooE»oo
U.9'i077E-02
".H1790E-02
O.OOUOOE+00
o.onocoE*oo
0.21940E-02
I.S1870E-02
U.OOUOOf»00
O.OOOOOE*00
0.'i0510E-OJi
O.OOUUOE+00
U.OOUOOE«00
0.'35000E*OU
P.91224E-0«!
'J.OOOOOE + OU
n.noooor»no
O.S2366E-02
n .OOUOOE+OO
n.OOOOOFtOO
0.f56525E-Oi:
0,OOOOOF»QO
0.67977E-02
O.OOOUOr.CO
O.OOOOOE+00
0.50540E-02
O.OPOOOE»00
0.10846E-01
O.OCOUOE+CO
0.7?356E-02
0.65300F.-02
O.OOOOOFtOO
0.92795E-02
O.OOUUOE4-OU
0.34720E-0;;
0.59850E-02
3.00000E+00
O.OOOOOE4-00
U.OUOOOE*00
O.OOUOOEtOO
O.OOOCOE*00
I.'.OOO:OE*OO
O.OOUOOE+00
O.»7760f-n2
0.57633E-02
U.OOOOOF «05
O.OOOUOEtOO
o.oooooc+oo
   LEGEND
        Column  1  is the state code which  corresponds  to that used
        in  Table  A-l.
        The columns of integers  preceeding  the  corresponding
        criteria  levels are the  number of points used in  computing
        that state average.
        For particulates and SOz,  the maximum observed 24-hr
        averages  were  used  in the  subsequent state average
        calculation.
        For N02,  the annual average  values  from individual stations
        were used to compute the  state average.

        For CO  and hydrocarbons,  the maximum observed 1-hr averages
        were used.
        A value of zero for a given  state indicates  unreported
        data.   For those points  we set x '/S = 1.0.
                                     39

-------
                        APPENDIX B
        EXAMPLE OF POPULATION SENSITIVE CALCULATION
1.
SOURCE INFORMATION
       Source Type;  Asphalt Paving-Hot Mix
     * Basic Data;  Table  B-l contains the basic data which
       will be used to  calculate the impact factor, I .
                                                      Jt
       Additional Data:
       Frequency of  operation (f)  = 0.17
       Total capacity  of  asphalt industry  (CAP) = 2.9478
       x 108 Mg/yr
       Number of materials emitted (N) = 7
       Height of emissions (h)  = 15.24
          Table B-l.  ASPHALT PAVING-HOT MIX INPUT DATA
Pollutant
Particulates
Sulfur oxides
Nitrogen oxides
Hydrocarbons
Carbon monoxide
POM3
Aldehydes
Primary
standard ,
g/m3
S = 2.6 x lQ~k
S2 = 3.65 x ID"4
S3 = 1.0 x ID"4
S4 = 1.60 x lQ~k
S5 = 4.00 x 10~2

TLV,
g/m3



TLV, = 5.1 x 10~6
b
TLV7 = 3.000 x 10~3
Emission factor,
g/Mg product
EI = 800.14
E2 = 400.07
E3 = 45.01
E. = 3.70
4
E = 5.00
E,. = 3.60 x 10~3
b
E? = 4.95 x 10"1
 POM = Polycyclic Organic Material.
                             40

-------
2.   PROCEDURE FOR CALCULATION OF IMPACT FACTOR
The equation used for determining impact factor is given as:
             K
[X   =   E
            N
           E
                            Fi
                                      X'i.
                 Si
                            1/2
                                                        (B-l)
For the asphalt industry having plants located in all 50
states and emitting seven pollutants, the above equation is
written as:
or
       50
zx  =  E
                           7
                           E
            Fi
              - p
7
E
              + P,
                          Fi
      lii
     F.
              Si
                             _ii
                              si
                       X'i.
                                      Si
                                           1/2
                                                     1/2
                                           1/2
                        50
        7
       E
                                         x1,
                                           i50
                             Fi
                                Si
                                                  1/2
This can be simplified as:
                                                        (B-2)
                                             '50
                            41

-------
where
I  = p.
 xl   -
 7

z
                              lil
                                        Y1
                                        x  i


                                        Si
                                              1/2
                                                        (B-3)
I   can be defined as the contribution  to  the  total  impact

 xl

factor I  by the 1st state, i.e., Alabama.   I    can  also  be
        X                                    X-*


written for the seven emitted  species as:
pi
V *u \
\F1 )
                            11
                                                21
                                     X'
                                       71
                          \
                                             1/2
                                                        (B-4)
To calculate the  total  impact  factor,  I  ,  it is necessary
                                       X

                                    '"s,
to the  impact  factor  by each state.
to first determine I  ,1   ,  	 I    , the contribution

                    xl   X2         X50
3.   CONTRIBUTION  TO  THE  IMPACT FACTOR BY THE FIRST STATE

     I    (ALABAMA)

      Xl
     Basic  Information  for  Alabama



     Stored data  for  state    :  01  (Alabama)

     Population fraction  PF,  =  1.69  x 10~2


     Population density P,    =  26.34 persons/km2




     Capacity  for Alabama (CAP,)


     CAP1' = (PF^ (CAP)


         -j^ = (1.69 x 10~2)(2.95  x  108)



         l = 4.985 x 106 Mg/yr
                             42

-------
c.   Emission rate for particulate for Alabama  (Q,)




     Q1 = j  (YPS) (CAP1) (E^
where:
           3.1688088 x 10"8 years

                   second
         ''Ql =  rTm3-17 x 10"8)(4-985 x  1Q6) (SOO.14)
           Q., = 743.47 g/sec
Dimensional analysis shows
           0  = [              x
           v      sec  /  year   Mg    sec
d.   X    for particulates for Alabama  (X     )
     —max	c	max, —
               2Q

     X
      maxl   7Th2eu
where:
        h2 =  (15.24)2 m2



        h2 =  232.26  m2



           _  	2  (734.47) g/m3
              (3.14)  (232.26)  (2.72)  (4.47)
     X     = 1.65 x 10'1  g/m-

      maxl



Dimensional analysis shows



     y     _ g x sec"1  _ g_


             m2(msec l)   m3
                            43

-------
e .   Hazard Potential Factor  (F.^ ) for particulates for Alabama

     Fx = S1 = 2.6 x 10'1* g/m3

     (All states have same F,)

f .   Other Pollutants for Alabama

Using the procedure described in Section 3. a through 3.c
above,  values for Q
                       max
                     and  F  are  calculated for all
pollutants from Alabama.  These values are then used to
calculate the impact factor for Alabama according to the
following formula:
                                                X'
                                                  21
                                                 S2
                                            1/2
                                                        (B-5)
where
[    =  impact  factor  contribution by each of seven
xl   .pollutants  from Alabama
P,  =  population  density of Alabama
    =  x     f°r  particulate in Alabama
      ITlcLX
    =  particulate ambient air level in Alabama
    =  2.24  x  10'^ g/m3
         F  '
         S  =
         F2 '
         S2 =
      hazard  potential factor for particulate
      primary standard for particulate
      X     for sulfur oxides in Alabama
      max
      sulfur  oxide  ambient air level in Alabama
      hazard  potential factor for sulfur oxides
      primary standard for sulfur oxide
                            44

-------
Other single digit subscripts identify specific pollutants
as listed in Table B-l, e.g., F-, F., FS/ F- and F_ refer to
the hazard potential factor for nitrogen oxides, hydrocarbons,
carbon monoxide, polycyclic organic material and aldehydes,
respectively.  In double digit subscripts, the first digit
identifies the pollutant as before, while the second digit
identifies the state, e.g., x~51» X52 and X53 refer to xmax
for carbon monoxide in Alabama, Alaska, and Arizona, respec-
tively.

g.   Impact Factor Contributions by All Seven Pollutants
     for Alabama

        X 11   ? ?4 v 1 o~ **
£>•___     J--L   f. , f.t A J.U     f> nr
Since,  —=— = 	 - u.ob
                2.6 x 10
then
and,
        X'
          11
   = 1.0
I  =
26.352
 1.65  x  10
V 2.6  x  10"
(1.0)
                                              •  * • • •
                                                     1/2
           x
   = ["(694.
  1  L
                     3) (633) +
                • • • • •  I
                                      1/2
          I  = 18,327  (i.e., the impact  factor contribution
           xl          for all seven pollutants  for Alabama)
Dimensional analysis shows
                 (persons/km2)
or
I   = persons/km2
 xl
                                                 1/2
                             45

-------
4.   CONTRIBUTION TO THE IMPACT FACTOR BY THE  SECOND  STATE
     (ALASKA)
a.   Basic Information for Alaska

     Stored data for state    :  02  (Alaska)
     Population fraction PF2  =  1.56 x  10~3
     Population density P_    =  2.14 x  10"1  persons/km2

b.   Capacity for Alaska  (CAP^)

     CAP2 = (PF2)(CAP)
     CAP2 = (1.56 x 10~3) (2.95 x 108)
     CAP2 = 4.60 x 105 Mg/year

c.   Emission rate for particulate  for  Alaska  (Qg)

     Q2 = ^T~   (YPS) (CAP2} (E1)

     Q2 = ^-Jy  (3.17 x 10~8)(4.60 x 105)(800.14)

     Q2 = 68.6 g/sec

d.   x    for particulate for Alaska  (X_    )
      ItlclX •            "   — •  -	   	^
                     2  (68.6)             ,  :
                                         g/m-
              (232.26) (3.14) (2.72) (4.47)
e.   Other Pollutants for Alaska

Similarly, Q2/ xmax  / and F  are calculated for all pollutants
from Alaska and these values are  used  to calculate the

                             46

-------
impact factor for Alaska using the following equation:
x, N2
substituting:
            (2.14 x
                       X'
                         12
                              + P.
'-  \2
 C22
X1
  22
                           X72
                           P.,
X'
  72
                                            1/2
                            ,2.60 x lQ~k
     I   = I 4.6 x 10"2  (59.6)2 +
      X2
                   (B-6)
     2      -i       1/2
       (1.0)


            1/2
where  I   = 15.5 = sum of impact factor contributions by
        X2 •         each of seven pollutants for Alaska.
5.   CONTRIBUTION TO THE IMPACT FACTOR BY THE REMAINING STATES

Using the same procedure as outlined above for Alabama and
Alaska, the respective contributions of each of the remain-
ing 48 states to the impact factor are calculated.  These
calculations will not be repeated, but follow by induction.
Therefore, the following relationship is achieved.
      X     1     O     O
Finally, for Asphalt Paving-Hot Mix,
     Ix = 3,221,290
                            47

-------
and, after rounding to one significant figure,





     I  = 3,000,000
      x




The input data form used for prioritization is shown in


Table B-2.
                            48

-------
                                      Table  B-2.
op-i
                    POPULATION SENSITIVE PRIORITIZATION DATA
       CATEGORY   Organic Chemicals
                       Log  No.	

                       Confidence
                       Leve1   B
       SOURCE DESCRIPTION  Asphalt Paving - Hot Mix


       SCC  3-05-002-99	.	
       SOURCE CAPACITY    2.9478 x 108
       FREQUENCY OF OPERATION
                                    17
               .Megagrams/year

               (% OF YEAR)
       NUMBER OF MATERIALS  EMITTED_

       NUMBER OF PLANTS/SITES
4800
       AVERAGE HEIGHT OF  EMISSION
                                       15.24
                                                      -Meters
MATERIAL EMITTED
PARTICIPATE
SOX
NOX
HC
CO
POM
Aldehydes



















TLV
(g/m3).





5.10 x 10"6
3.00 x 10"3



















EMISSION FACTOR
(g/Mg)
800.14
400.07
45.01
3.70
5.00
3.60 x 10~3
4.95 x 10"1



















REFERENCE
Vandegrift, A.E., et al.
"Particulate Emission Syst.
Study." Volume I - Mass
Emissions. MRI. NTIS
# PB203-128
Hangebrauch, R. P.,
VonLehmden, D. J. , and
Meeker, J. E. "Sources of
Polynuclear Hydrocarbons in
the Atmosphere." Environmental
Health Series. AIR-136.
PB 174706

MRC Engineering Estimates












                                            49

-------
                        APPENDIX C

              LOCATION SENSITIVE CALCULATIONS
1.   SOURCE INFORMATION

     • Source Type:  Coal-Fired Steam Electric Utilities

     • Input Data;

          Total Capacity (CAP) = 3.9 x 108 Mg/yr coal burned
          Frequency of operation (f) = 1.0
          Number of materials emitted (N) = 19
          Height of emission  (h) = 82.3 m
2.
IMPACT FACTOR CALCULATION
The following equation will be used to calculate the impact
factor for the first state:
         = Pi
                19
                                1/2
                                                  (C-l)
Since there are 19 materials emitted in each of the states
the calculations will be shown for only three materials
(particulate, sulfur oxides, and aldehydes) in one state
(Alabama),  and the remaining calculation steps follow by
induction.
                            50

-------
a.   Data for First State:  01  (Alabama)


     Population density  (Pi) =  26.3 persons/km2

     Capacity  (CAP^ = 1.842 x  10 7 Mg/yr

     X'n = 2.24 x 10"1* g/m3

     X'21 = 1.08 x 10"5 g/m3



b.   For Particulates


     Emission factor  (E,) = 15,600 g/Mg of coal  burned


       Ql =(|)(YPS) (CAPi) 
       Q1 =        (3.17 x 10~8  ) (1.842  x  107)(15,600)
          = 9,109 g/sec


              2Q
     Xmax = TTH'eu
                       2  (9109)
      max    (3.14159)16773.3) (2.72) (4.47)


          =  °-0705 ^/m3

                       x'
Defining A  =
          X 11                   X  -11
and since -5 — <  1.0,  then set  -5 — =1.0
           Sl                     Sl

                     07052
               2.60 x



            = 73524
                             51

-------
c.   For Sulfur Oxides
     SO  emission factor  (E9)  =  4.75  x 101* g/Mg
          Q2 =y(YPS) (CAP^ (E2)
             =  j     (3.17  x 10"8) (1.842 x 107)(4.75 x





             = 27,736  g/sec
         max   Treuh2





                  (2) (27736)
                (38.43) (82.3) 2






             =  0.213  g/m3







               /7   \  2 /v1    \
               / X21 l   I  *  21  1
Defining  A  = U^     -5^

           ^   \F2  /   \ S2   /





                /    0.213    \2
                 3.65  x  10
                                (1.0)
          A2 =  340544
d.   For Aldehydes





     Aldehyde emission  factor (Eg)  = 2.5 g/Mg
          Q  =      (YPS) (CAP^ (Eg)
                      (3.17  x 10~8) (1.842 x 107) (2.5)






          Q_ = 1.46  g/sec








                             52

-------
        x    =      (2)(1.46)

         max     (38.43)(82.3)2
                               3
        *max = 1-12 x lO'* g/m
                     2

               X71 \   / X'
Defining A  = I -j±.
          I   \ * -i
Since S7 is undefined for aldehydes, then;
and
Since aldehyde TLV = 3 x 10~3 g/m3


then            F? = (3 x 10~3)(2.38 x 10~3)


                F? = 7.14 x 10"6 g/m3


 «*             A    /1.12 x 10"5 \ 2  M n,
and             A_ = /	  ]   (1.0)
                     V7.14 x 10~6
                A? = 2.46
then
                                                           1/2
                            + A  +  ---- + A  +  ---- + A)  '
               I   =  (26.3) (73524. + 340544. +  ...  +  2.5  +  ..
                Xl
               I   = 50,421
                Xl
                            53

-------
The above procecure is repeated for the remaining states


to obtain:
           I  = 50421 + 	 + I
            x
           I  = 2,289,560
            j£





and after rounding,






           I  = 2,000,000
            JC





The input data forms used for the above location sensitive


calculations are shown in Tables C-l through C-3.
                            54

-------
                            Table C-l.
CATEGORY
             LOCATION  SENSITIVE PRIORITIZATION DATA   Pa9e I of 1
                                                     Confidence
                                                     Level	B
              Combustion
SOURCE DESCRIPTION  Coal-Fired Steam Electric Utilities

SCC	'_	

TOTAL PRODUCTION  4.30 x 108	____
 (Fuel Consumption!
FREQUENCY OF OPERATION     100	

NUMBER OF PLANTS/SITES	
.(TONS/YEAR)

 (%  OF  YEAR)
NUMBER OF MATERIALS EMITTED
                                 19
MATERIAL EMITTED
PARTICULATE
SOX
NOX
HC
CO
Aldehydes
Arsenic
Beryllium
Manganese
Mercury
Nickel
Vanadium
Barium
Boron
Cadmium
Copper
POM
Selenium
Zinc








TLV
(g/m3)





3 x 10~3
5 x lO""*
2 x 1C"6
5 x 10~3
1 X 10~5
1 x 10"
5 x 10"
_i<
5 x '10
10 x 10"
1 x lO"*1
1 x 10~3
10 x 10"6
2 x io"1*
5 x 10~3








EMISSION
FACTOR
(Ibs/ton)
31.2
95.0
18
0.3
1.0
0.005
3 x IO"3
3.7 x IO"3
a x io"2
4 x 10'1*
-it
6 x 10
-4
7 x 10
15 x 10~3
18 x IO"3
1 x IO"3
2.5 x IO"3
1.4 x 10~6
2.5 x IB"3
17 x 10" 3








AVG.
EMISSION
HEIGHT (ft)
270
i















\
t















t
270








REFERENCE



























                                 55

-------
                                Table  C-2.
OF 2a
LOCATION SENSITIVE  PRIORITIgATION DATA
           STATE  INFORMATION
                                                            Page 2 of 3
      SOURCE DESCRIPTION_

      AVERAGE PLANT SIZE

      NUMBER OF STATES
                          Coal-Fired Steam-Electric Utilities
                             (TONS/YEAR)
            42
STATE
CODE
(XX)
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31

STATE PRODUCTION
(TONS/YEAR)
2.03 X 107
5.02 x 103
5.23 x 105
0
0
5.12 x 106
3.24 x lO1*
9.53 x 10s
7.4 x 106
1.21 x 107
0
0
3.63 x 107
3.00 x 107
5.92 x 106
1.16 x 10«
7.50 x 107
0
0
4.60 x 10s
1.45 x 1011
2.29 x 10 7
7.71 x 106
1.34 x 10 6
1.74 x 10 7
9.97 x 10 5
1.50 x 10 6
4.31 x 10 6
1.16 x 10 6
2.66 x 106
8.38 x 10 6

NUMBER
OF
PLANTS
































REFERENCE

























,






                                     56

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                              Table  C-3.
OF- 2a
LOCATION SENSITIVE  .•HIORITIi'.ATJ i_N UATA
           STATE INFORMATION
                                                            Page 3 of 3
      SOURCE DESCRIPTION Coal-Fired Steam Electric  Utilities

      AVERAGE PLANT SIZE	(TONS/YEAR)

      NUMBER OF STATES	
STATE
CODE
(XX)
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50













STATE PRODUCTION
(TONS/YEAR)
6.50 x 106
2.22 X 107
5.39 x 106
4.86 x 107
2.23 x 103
0
4.34 x 107
0
6.10 x 106
4.01 x 105
1.95 x 107
5.28 x 106
1.10 x 106
3.35 x 101*
5.51 x 106
4.17 x 106
2.54 x 107
1.13 x 107
6.47 x 106













NUMBER
OF
PLANTS
































REFERENCE
































                                     57

-------
                        APPENDIX D
              EXAMPLE OF DETAILED CALCULATION
1.   SOURCE INFORMATION

     •  Source Type;  Acrylonitrile Manufacturing

     •  Input Data for all Plants

          Total Capacity (CAP)  = 530706 Mg
          Frequency of operation (f) = 1.0
          Number of emitted materials (N)  = 10
          Height of emissions (h)  = 30.5 m
Material
emitted
Particulate
SO
X
N0x
CO
Acrylonitrile
Acetonitrile
Hydrogen cyanide
Propylene
Propane
Lube oil
TLV,
g/m3


0.045
0.070
0.011
1.88
1.97
0.067
Emission
factor,
g/Mg
20.0
26,000.0
7,300.0
178,500.0
9,500.0
9,000.0
1,300.0
101,000.0
140,000.0
3,550.0
Emission
height,
m
30.5
H
ii
ii
H
ii
ii
H
n
11
                            58

-------
        Input Data for Plant 1

          Plant capacity  (CAP^ = 81647 Mg/yr
          County population density  (P, ) = 1103 persons/km2

2.   IMPACT FACTOR CALCULATION

The emission rate for particulates  (Q,) is calculated as
follows:
     Ql =  ?   (YPS) (CAPl) {s
                 (3.17 x 10"8) (81647) (20)
     Q, = 0.0518 g/sec

               (2) (0.0518)
    maxl     (38.43) (30.50)2

         ' 2'9 x 10"6 */m3
Defining A  -
               F1
The first plant is in Louisiana, and from Table A-2,  x'  -
1.73 x 10~u g/m3), and since x'/S < 1.0, we  set this  ratio
x'/s = i.o.

               /2 92 x 10~6 \ 2
Then,     A, = /   ^ x  u— |    (1.0)
           1   \2.6 x 10'*  /

          A, = 1.24 x lQ~k
                            59

-------
and for acrylonitrile:






     Emission factor  (E5) :   9500 g/Mg



     TLV = 0.045 g/m3
      F5 = 1.07 x 10"4 g/m
      Q5 =       (3-17 x 10"8) (81647) (9500)
      Q5 = 24.6 g/sec






           =    (2) (24.6)


      maX5     (38.43) (30. 5)2
     *max5 = 1-38 x 10-3 g/m3






Since S is undefined for acrylonitrile, we set:






                            = 1.0
                         &






                /x  \2
and define Ac =  =^i   (1.0)
           a  _ . 1-38 X

           A5 ~
                 1.07 x
           A5 = 166.





This process is repeated for the ten emitted materials and


the impact factor for the first plant is:
                             60

-------
     I   =  (1103)  [1.94 x lQ~k +  ... -I- 166 +  ... AirJ1/2
      x                                           x u
     I   =  (1103) [551]1/2
      Xl
     I   = 25,891
      Xl
The data for the next plant capacity and county population
density are then read and the process continues in the  same
fashion until all five impact factors are computed.  The
final impact factor is then:
          I  = 25,891 + ... + I
           J\.                   ** f
          Ix = 41,709
and after rounding

          I  = 40,000
           A

Detailed input data used in this calculation  are  presented
In Tables D-l through D-5.
                            61

-------
                                 Table  D-l.
l-F-3
      CATEGORY
                     DETAILED INPUT PRIORITIZATION DATA


                     Organic
                                                            Log No.   1005
            Uncertainty
            Level^	 B
      SOURCE DESCRIPTION	


      scc          3-01-026-08
                             Acrylonitrile
      SOURCE IDENTIFICATION   American Cyanamide, Fortier, La.
      SOURCE CAPACITY	90.000
      (PRODUCTION,  FUEL USAGE)

      FREQUENCY OF OPERATION   	_1.0
        (TONS/YEAR)
      NUMBER OF HAZARDOUS  MATERIALS  EMITTED

      COUNTY POPULATION DENSITY     2857
10
                                                       (PERSONS/SQUARE MILE)
MATERIAL EMITTED
PARTICULATE
SOX
NOX
HC
CO
Acrylonitrile
Acetonitrile
Hydrogen Cyanide
Propylene
Propane
Lube Oil















TLV
(g/m3)





0.045
0.070
0.011
1.88
1.97
0.067















EMISSION
FACTOR
(Ibs/ton)
0.04
52.0
14.6

357
19.0
18.0
2.6
202.
280.
7.1















AVG.
EMISSION
HEIGHT (ft
100
100
100

100
100
100
100
100
100
100















AMBIENT CONC.
(g/m3)














•











REFERENCE


























                                       62

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                                    Table  D-2.
IT-3
      CATEGORY
                     IHvTAILED INPUT PRIORITIZATJON DATA


                     Organic
                                                            Log No.   1005
                                        Uncertainty
                                        Level
      SOURCE DESCRIPTION     Acrylonitrile


      SCC
3-01-026-08
      SO.URCE IDENTIFICATION   DuPont,  Memphis,  Tennessee
      SOURCE CAPACITY	81,000
      (PRODUCTION, FUEL USAGE)
      FREQUENCY OF OPERATION       1.0
                                    (TONS/YEAR)
      NUMBER OF HAZARDOUS MATERIALS EMITTED      1Q

      COUNTY POPULATION DENSITY	962	
                                    (PERSONS/SQUARE MILE)
MATERIAL EMITTED
PARTICULATE
SOX
NOX
IIC
CO





















TLV ,
(g/m3)


























EMISSION
FACTOR
(Ibs/ton)


























AVG.
EMISSION
HEIGHT (ft)


























AMBIENT CONC.
(g/m3)


























REFERENCE


























                                         63

-------
                                 Table D-3.
l'F-3
      CATEGORY
                     III'TAILED INPUT PRI01UTIZATION DATA
                     Organic
                                                            Log No.   1005
                                        Uncertainty
                                        Level	B_
      SOURCE DESCRIPTION     Acrylonitrile

      sec
3-01-026-08
      SOURCE IDENTIFICATION	DuPont, Beaumont,  Texas
      SOURCE CAPACITY	90,000
      (PRODUCTION, FUEL USAGE)

      FREQUENCY OF OPERATION       1.0
                                    (TONS/YEAR)
      NUMBER OF HAZARDOUS MATERIALS  EMITTED      1Q

      COUNTY POPULATION DENSITY        255
                                                       (PERSONS/SQUARE MILE)
MATERIAL EMITTED
PARTICULATE
SOX
NOX
I1C
CO





















TLV
(g/m3)


























EMISSION
FACTOR
(Ibs/ton)


























AVG.
EMISSION
HEIGHT (ft)


























AMBIENT CONC.
(g/m3)


























REFERENCE


























                                    64

-------
                               Table D-4.
l'F-3
      CATEGORY
                     DETAILED INPUT PRIOIUTIZATION  DATA


                     Organic
                                                            Log  No.   1005
                        Uncertainty
                         Level	B_
      SOURCE DESCRIPTION	


      scc          3-01-026-08
                             Aerylonitrile
      SOURCE IDENTIFICATION    Monsanto, Chocolate Bayou, Texas
      SOURCE CAPACITY	
      (PRODUCTION, FUEL USAGE)

      FREQUENCY OF OPERATION
                                       166,000
                    (TONS/YEAR)
1.0
      NUMBER OF HAZARDOUS MATERIALS  EMITTED

      COUNTY POPULATION DENSITY	75
             10
                    (PERSONS/SQUARE  MILE)
MATERIAL EMITTED
PARTICULAR'S
SOX
NOX
IIC
CO





















TLV
(g/m'3)


























EMISSION
FACTOR
(Ibs/ton)


























AVG.
EMISSION
HEIGHT(ft)


























AMBIENT CONC.
(g/m3)


























REFERENCE


























                                     65

-------
                                  Table  D-5.
l-F-3
      CATEGORY
                     Dl'TAILED INPUT PRIOH ITI7.ATION DATA


                     Organic
                                                            Log No.  1005
                          Uncertainty
                          Level	n_
      SOURCE DESCRIPTION	

      scc           3-01-026-08
                             Acrylonitrile
      SOURCE IDENTIFICATION	


      SOURCE CAPACITY	
      (PRODUCTION, FUEL USAGE)

      FREQUENCY OF OPERATION
Vistron. Lima, Ohio
  158.000
(TONS/YEAR)
  1.0
      NUMBER OF HAZARDOUS MATERIALS FJ1ITTED

      COUNTY POPULATION DENSITY       270
              10
                                                       (PERSONS/SQUARE MILE)
MATERIAL EMITTED
PAKTICULATE
SOX
NOX
ilC -
CO





















TLV
(g/m3)


























EMISSION
FACTOR
(Itos/ton)


























AVG.
EMISSION
HEIGHT(ft)


























AMBIENT CONC.
(g/m3)


























REFERENCE


























                                        66

-------
                        APPENDIX E
            EXAMPLE OF OPEN SOURCES CALCULATION

1.    APPROACH

In almost all cases, open sources were found to emit
particulates.  These emitted particulates vary widely in
composition among the various source types.  Thus, instead
of substituting the primary standard for the potential
hazard factor, a composite TLV was computed using the
following:
                            1'°     -                   (E-l)
                         N      f
                         £      -^
                         /^     TLV..^
where ,            N
                      f
                       c.
          TLV  = composite TLV, g/m3

          f    = fraction of i— component

          TLV. = threshold limit value of the i— component,
                 g/m3
             N = number of components

                            67

-------
Since there is only one emitted material, the impact
factor equation reduces to:
                                                       (E-2)
where, S = particulate standard = 2.6 x lQ~k g/m3.

For ground level releases  (h=0), the Gaussian Plume equation
reduces to:
                    X =
It is obvious that there is no maximum concentration for a
ground level release.  Two options were available to avoid
this problem.  The first method would be to select an
average constant distance from source to receptor.  In a
relative rank ordering, this constant distance could be
arbitrary since it would only affect the magnitudes of the
impact factors and not their order.  Another approach was
to select an arbitrary imaginary height and use the x
equation.  This latter approach was used to preserve
computational compatibility with other source type calcu-
lations.

For open source location sensitive calculations, the
production capacity on a single county or multi-county
basis was known.  For a given state, the population in the
affected counties was summed and divided by the sum of the
county areas in order to compute the population density of
the j— region.

As can be seen from the input data sheet  (Table E-l), the
sum of the state capacities does not equal the U.S. total
                            68

-------
capacity.  To preserve the confidentiality of individual
manufacturers' production data, the Minerals Yearbook does
not publish data for states with only a few individual manu-
facturers.  These data are included in the national total
as unreported capacity.

For these calculations, the last stage in computing I  is
as follows:

        _  	.	Impact factor	
      x    (Sum of reported quantity handled/total U.S. quantity)

2.   SOURCE INFORMATION

     • Sample Type;  Barite Milling

     • Composite TLV (TLV )

Particulate consists of 92% Barite  (BaSO^) with a TLV of
0.5 x 10~3 g/m3 and 8% inert dust with a TLV of 1.0 x 10"2
g/m3.  Therefore,
                                    1.0
                  =         ~                  """~
        composite ~~  inert fraction   BaSOi^ fraction
                       TLVinert        TLV
             TLV  =  -
                c       0.92      .   0.08
                     0.5 x 10~3    1 x 10~2
             TLVc = 0.54 x 10~3 g/m3
                            69

-------
        Input Data;

          Total U.S. Capacity  (CAP):  1,466,926  Mg/year
          Emission height  (h):  3.05 m

Other data' are presented in Table E-l.
      Table E-l.  PRIORITIZATION DATA  (OPEN SOURCES)
SOURCE:  Barite Milling
TOTAL U.S. QUANTITY:  1,466,926
AVERAGE HEIGHT:  3.05 meters
DISTRIBUTION:  POP      AREA
  FREQUENCY:  1.0
  UNITS:  Megagrams

LOG  /
Location
18
25
43
28
4
Total
Quantity
handled,
Mg
459,945
210,468
181,438
174,181
154,222
1,180,254
Emission
factor,
g/Mg
2,500
it
H
M
H

Composite
TLV,
g/m3
0.54 x 10"3
H
H
H
H

Population,
people
585,787
15,015
2,093,840
2,630
21,498

Area,
km2
531
1,968
8,972
14,558
1,608

3. IMPACT FACTOR CALCULATION

a.   For State 18  (Louisiana)

     Capacity  (CAP^ = 459,945 Mg/yr

     Population density  (P,) =  (585787) (0.3858)

                             = 1,102 persons/km2

     X1 for particulates = 1.73 x 10"1* g/m3
                            70

-------
     Frequency of operation  (f)  =  1.0




     Emission factor  (E) = 2,500 g/Mg
and
        Q-L = (— )  (E) (CAP^ (YPS)






where  YPS = 3.17 x  10~8  years/second
        Ql =JL-(250°) (459945) (3-17 x 10~8)
        Q, = 36.5 g/sec




           =     (2)(36.5)


       max    (38.43) (3.05)2
      X    = 0.204  g/m3
      Amax          ^'
and                     •    1/2
           = P
             Pl  F
where    F =  (0.54  x  10~3)(40/168)(1/100)




         F =  1.29 x 10~6  g/m3





           =  (1102)
        xl          \1.29  x 10~6
       I   = 1.75  x  101

        xl
                             71

-------
b.   For State 25  (Missouri)




       X1 = 2.06 x 10~" g/m3


     • V '
    • .*- = 1.0



     CAP2 = 210,468 Mg/year



         f = 1.0



        E = 2500 g/Mg



       P_ = 7.6 persons/km2
       Q2 = (Y-%)  (2500) (210468) (3.17  x 10~8)


       Q2 = 16.68 g/sec


              (2) (16.68)

    Xmax2   (38.43)(9.3)




    xmax  = 9'3  X 10~2 g//m3



and


      I   = 7.6  /-9-'-3 x 10~2
       X2       \1.29 x  10~6


      I   = 5.5 x 105

       X2
c.   For State 43  (Texas)




       X1 = 2.3 x  I0~k g/m3


     . Y '
    • -|- = 1.0



     CAP3 = 181,438 Mg/year



         f = 1.0



       P, = 234 persons/km2




       Q3 = (j7§)  (181438) (2500) (3.17  x 10"8)



       Qo = 14.4 g/sec




                             72  •

-------
             28.8
             357.4
     Xmax3 = 8.06 x 10~2


       !   = 234 /8.06 x IP"2
     •   X3       \1.29 x 10"6
       I   = 1.46 x 107
        X3
d.   For State 28  (Nevada)


      CAP4 = 174,181 Mg/yr


        ?4 = 0.18 persons/km2


        X1 = 3.74 x 10~"

             3.74 x 10"
        S    2.60 x lO""
                         = 1.054
        Q4 =  (2500) (174181) (3.17 x  10""8)

        Q4 = 13.8 g/sec
     Xmax. = 7.7 x 10 2 g/m3

         4             ,, x  1/2
           =  (PJUr1
               4'\F /\ S
       I   =  (0.18)(5.97 x 10k) (1.03)
        X4
      I   = 1.1 x 10k
       X4
e.   For State 4  (Arkansas)


      CAP5 = 154,222 Mg/yr


        PS = 13.4 persons/km2

        X1 = 1.5 x 10"" g/m3

                            73

-------
        Q5 = 12.2 g/sec

           = 6.9 x 10^
       I   =  (13.4)(5.4 x 104)(1.0)
        X5

       I   = 7.24 x 105
        X5

        I  =1   +  . . . + I
         X    X,          X,.


        Ix = 1.91 x 108



Since the reported totals are  80.5% of the U.S. total
capacity,
             1.91 x 10
                      8
         x     0.805
        I  = 2.37 x 108
         X
                            74

-------
                        SECTION IV

                        REFERENCES
1.   Turner, D. B.  Workbook of Atmospheric Dispersion
     Estimates.  Publication No. 191482, May 1970.

2.   Eimutis, E. C., and M. G. Konicek.  Derivations of
     Continuous Functions for the Lateral and Vertical
     Atmospheric Dispersion Coefficients.  Atmospheric
     Environment, 6_: 859-863, 1972.

3.   Slade, H. S.  (ed.).  Meteorology and Atomic Energy.
     Publication TID 24190, July 1968.

4.   The World Almanac Book of Facts, 1974.

5.   Air Quality Data - 1972 Annual Statistics.  Publication
     No. EPA-450/2-74-001.
                            75

-------
                                 TECHNICAL REPORT DATA
                          (Please read Instructions on the reverse before completing)
 1. REPORT NO.
 EPA-600/2-76-032a
                            2.
                                 3. RECIPIENT'S ACCESSION-NO.
 4. TITLE AND SUBTITLE
  Source Assessment: Prioritization of Stationary
     Air Pollution Sources--Model Description
                                 5. REPORT DATE
                                  February 1976
                                 6. PERFORMING ORGANIZATION CODE
 7. AUTHOH(S)

  Edward C. Eimutis
                                                       8. PERFORMING ORGANIZATION REPORT NO.
                                  MRC-DA-508
 9. PERFORMING ORGANIZATION NAME AND ADDRESS
  Monsanto Research Corporation
  1515 Nicholas Road
  Dayton, Ohio  45407
                                 10. PROGRAM ELEMENT NO.
                                 1AB015; 21AVA-003
                                 11. CONTRACT/GRANT NO.
                                  68-02-1874
 12. SPONSORING AGENCY NAME AND ADDRESS
  EPA, Office of Research and Development
  Industrial Environmental Research Laboratory
  Research Triangle Park, NC  27711
                                 13. TYPE OF REPORT AND PERIOD COVERED
                                 Task Final; 3/75-10/75
                                 14. SPONSORING AGENCY CODE
 15. SUPPLEMENTARY NOTEsEpA_650/2-75-019a was the first report in this series.

  EPA project officer for this report is D.A. Denny, 919/549-8411, Ext 2547.
 16. ABSTRACT
           The report describes a prioritization model for the rank-ordering of
  stationary air pollution sources. The source types were rank-ordered or prior-
  itized by computing a relative environmental impact factor for each source type.
  A priority listing was developed for each of four categories:  combustion, organic
  materials, inorganic materials, and open sources.  The report also describes both
  the actual application of the model and the types of calculations that were performed
  depending upon the degree of input  aggregation.  The report also gives detailed
  examples of use, as well as results of sensitivity analyses, showing how the
  prioritization model responds to input changes.
                             KEY WORDS AND DOCUMENT ANALYSIS
                 DESCRIPTORS
 Air Pollution
 Order (Sequence)
 Mathematical Models
 Environmental Engineering
 Combustion
 Organic Compounds
Inorganic Compounds
 3. DISTRIBUTION STATfcMENT
 Unlimited
                                          b.lDENTIFIERS/OPEN ENDED TERMS
Air Pollution Control
Stationary Sources
Pollutant Sources
Environmental Impact
Open Sources
                                           19. SECURITY CLASS (ThisReport}
                                          Unclassified
                     20. SECURITY CLASS (This page I
                     Unclassified
                                              c.  COSATi Field/Group
13B
12A

05E
2 IB
07C
07B
                                              21. NO. OF PAGES
                                                   83
                                              22. PRICE
EFA Form 2220-1 (9-73)
                                          77

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