United States
Environmental Protection
Agency
Industrial Environmental Research
Laboratory
Research Triangle Park NC 27711
EPA-600/2-78-004r
July 1978
Research and Development
Source Assessment:
Overview Matrix for
National Criteria
Pollutant Emissions
(1978)
-------
RESEARCH REPORTING SERIES
Research reports of the Off ice of Research and Development, U.S. Environmental Protec-
tion Agency, have been grouped into nine series. These nine broad categories were
established to facilitate further development and application of environmental tech-
nology. Elimination of traditional grouping was consciously planned to foster technology
transfer and a maximum interface in related fields. The nine series are:
1. Environmental Health Effects Research
2. Environmental Protection Technology
3. Ecological Research
4. Environmental Monitoring
5. Socioeconomic Environmental Studies
6. Scientific and Technical Assessment Reports (STAR)
7. Interagency Energy-Environment Research and Development
8. "Special" Reports
9. Miscellaneous Reports
This report has been assigned to the ENVIRONMENTAL PROTECTION TECHNOLOGY
series. This series describes research performed to develop and demonstrate instrumen-
tation, equipment, and methodology to repair or prevent environmental degradation from
point and non-point sources of pollution. This work provides the new or improved tech-
nology required for the control and treatment of pollution sources to meet environ mental
quality standards.
REVIEW NOTICE
This report has been reviewed by the U.S. Environmental
Protection Agency, and approved for publication. Approval
does not signify that the contents necessarily reflect the
views and policy of the Agency, nor does mention of trade
names or commercial products constitute endorsement or
recommendation for use.
This document is available to the public through the National Technical Informa-
tion Service, Springfield, Virginia 22161.
-------
EPA-600/2-78-004r
July 1978
Source Assessment:
Overview Matrix for National
Criteria Pollutant Emissions
(1978)
by
E.G. Eimutis, R.P. Quill, and G.M. Rinaldi
Monsanto Research Corporation
1515 Nicholas Road
Dayton, Ohio 45407
Contract No. 68-02-1874
ROAPNo. 21AXM-071
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
-------
PREFACE
The Industrial Environmental Research Laboratory (IERL) of the
U.S. Environmental Protection Agency (EPA) has the responsibility
for insuring that pollution control technology is available for
stationary sources to meet the requirements of the Clean Air Act,
the Federal Water Pollution Control Act, and solid waste legis-
lation. If control technology is unavailable, inadequate, or
uneconomical, then financial support is provided for the develop-
ment of the needed control techniques for industrial and extrac-
tive process industries. The Chemical Processes Branch of the
Industrial Processes Division of IERL has the responsibility for
investing tax dollars in programs to develop control technology
for a large number of operations (more than 500) in the chemical
industries.
Monsanto Research Corporation (MRC) has contracted with EPA to
investigate the environmental impact of various industries which
represent sources of pollution in accordance with EPA's respon-
sibility as outlined above. Dr. Robert C. Binning serves as MRC
Program Manager in this overall program entitled "Source Assess-
ment", which includes the investigation of sources in each of
four categories: combustion, organic materials, inorganic
materials, and open sources. Dr. Dale A. Denny of the Industrial
Processes Division at Research Triangle Park serves as EPA Pro-
ject Officer. Reports prepared in this program are of three
types: Source Assessment Documents, State-of-the-Art Reports,
and Special Project Reports.
Source Assessment Documents contain data on emissions from spe-
cific industries. Such data are gathered from the literature,
government agencies, and cooperating companies. Sampling and
analysis are also performed by the contractor when the available
information does not adequately characterize the source emis-
sions. These documents contain all of the information necessary
for IERL to decide whether emissions reduction is required.
State-of-the-Art Reports include data on emissions from specific
industries which are also gathered from the literature, govern-
ment agencies, and cooperating companies. However, no extensive
sampling is conducted by the contractor for such industries.
Results from such studies are published as State-of-the-Art
Reports for potential utility by the government, industry, and
others having specific needs and interests.
111
-------
Special projects provide specific information or services which
are applicable to a number of source types or have special uti-
lity to EPA but are not part of a particular source assessment
study. This special project report, "Source Assessment: Over-
view Matrix for National Criteria Pollutant Emissions", was
prepared to provide an updated alphabetical listing of stationary
sources that emit criteria pollutants. A similar listing was
generated and published earlier.
IV
-------
ABSTRACT
This report provides an overview matrix or alphabetical listing
of stationary sources that emit criteria pollutants. The matrix
shows the relative importance of source types in terms of their
effect on the total national emissions burden and overall ambient
air quality. A source type is defined as a group of emission
sources which have the same process and emission characteristics.
The overview matrix was prepared using a computerized data base
established for emissions of air pollutants from approximately
800 stationary source types in the combustion, organic materials,
inorganic materials, and open source categories. Emissions
included in the data base consist of criteria pollutants (i.e.,
particulates, sulfur dioxide, nitrogen oxides, hydrocarbons, and
carbon monoxide) and noncriteria pollutants (such as trace metals
and polycyclic organic matter). The data base is updated con-
tinuously to incorporate related new findings and covers a large
number of source types; however, it is not an exhaustive list of
all stationary emission points in the United States.
This report was submitted in partial fulfillment of Contract 68-
02-1874 by Monsanto Research Corporation under the sponsorship of
the U.S. Environmental Protection Agency. This updated listing
is similar to those generated for internal EPA use in July 1975,
July 1976, and September 1976, and it supersedes a document of
the same title published in July 1977 (EPA-600/2-77-107c). This
report was prepared during the period April - July 1978.
v
-------
CONTENTS
Preface iii
Abstract v
Symbols viii
1. Introduction
2. Overview Matrix for National Criteria Pollutant
Emissions
References 67
VII
-------
SYMBOLS
C — code number which identifies the source category
CO — carbon monoxide
HC — hydrocarbons
NOX — nitrogen oxides
PART — particulates
S02 — sulfur dioxide
Vlll
-------
SECTION 1
INTRODUCTION
During the performance of the Source Assessment Program for EPA
on Contract 68-02-1874, a computerized data base was established
for emissions of air pollutants from approximately 800 stationary
source types in the combustion, organic materials, inorganic
materials, and open source categories. A source type is defined
as a group of emission sources which have the same process and
emission characteristics; e.g., rubber processing, beef cattle
feedlots, etc. Emissions included in the data base consist of
criteria pollutants (i.e., particulates, sulfur dioxide, nitrogen
oxides, hydrocarbons, and carbon monoxide) and noncriteria pollu-
tants (such as trace metals and polycyclic organic matter).
The data base is updated continously to incorporate related new
findings from the investigation of individual emission source
types on this program. Although the data base covers a large
number of source types, it is not an exhaustive list of all
stationary emission points in the United States. The source list
was selected to cover over 90% of the emissions in those areas
under the original jurisdiction of EPA's Chemical Processes
Branch at IERL-RTP. In other areas, such as metallurgical pro-
cesses, some additional source types were later added to the data
base to provide a better coverage of national emissions. How-
ever, this coverage is by no means as complete as that for the
four categories selected for intensive study.
Using the above computerized data base, this overview matrix was
prepared to provide an alphabetical listing of stationary source
types and their national total emissions of criteria pollutants.
The matrix shows the relative importance of source types in terms
of their effect on the total national emissions burden and over-
all ambient air quality. A detailed state-by-state listing of
stationary emission sources which emit at least 1% of each
state's total mass emissions of any criteria pollutant is given
in a separate report entitled "Source Assessment: State-by-State
Listing of Criteria Pollutant Emissions". Mass emissions of
noncriteria pollutants from various stationary sources are given
in a separate report entitled "Source Assessment: Noncriteria
Pollutant Emissions".
-------
The following explanatory remarks are provided for this report:
1. All emissions are expressed as 103 kg/yr
(metric ton/yr).
2. Every computer-printed page lists criteria
as PART (particulates), S02 (sulfur dioxide),
NOX (nitrogen oxides reported as N02)/ HC
(hydrocarbons), and CO (carbon monoxide).
3. The last column, designated C, identifies the
source category as follows:
Code Category
1 Combustion Sources
2 Organic Materials Sources
3 Inorganic Materials Sources
4 Open Sources
4. The national emission totals for all the criteria
pollutants are listed both as calculated from our
computerized data base and as obtained from the
National Emissions Data System (NEDS)(1), which
includes mobile as well as stationary sources.
The totals have been adjusted to include New
York point sources, forest wild fires, agricul-
tural open burning, structural fires, coal refuse
fires, and metallurgical processing.
5. Line one for each source type shows the annual
mass of emissions of each criteria pollutant.
Line two shows the percent contribution of each
source type to the total amount of each criteria
pollutant emitted from all stationary sources
(i.e., as reported in our computerized data base).
Line three shows the percent contribution to
emissions from both stationary and mobile sources
(i.e., NEDS).
6. All emissions data are rounded to four signifi-
cant figures; percentages are rounded to three
significant figures.
7. For source types that emit less than 100 kg of
each criteria pollutant, dashes (—) are shown
for all emissions.
(1) National Emissions Report, 1972. EPA-450/2-74-012, U.S.
Environmental Protection Agency, Research Triangle Park,
North Carolina, June 1974. 422 pp.
-------
8. Hydrocarbon totals for each source type include
unnamed hydrocarbons and all named nonmethane
organic materials.
9. Particulates are the only criteria pollutant considered
in this overview matrix for open sources. When that
column is blank, it indicates that no particulates are
emitted.
10. The overview matrix presented in this report is based
on the data base contents as of 1 July 1978.
Example;
Coke manufacture emits the following amounts of criteria
pollutants:
Particulates: 218,200 x 103 kg/yr
S02: 161,700 x 103 kg/yr
NOX: 1,581 x 103 kg/yr
Hydrocarbons: 167,600 x 103 kg/yr
Carbon monoxide: 50,200 x 103 kg/yr
Criteria pollutants emitted by coke manufacture contribute
the following portions of the total amounts of such pollu-
tants emitted from all stationary sources in the United
States (as contained in the data base):
Particulates: 0.174%
S02: 0.704%
NOX: 0.0149%
Hydrocarbons: 1.44%
Carbon monoxide: 0.0563%
Criteria pollutants emitted by coke manufacture contribute
the following portions of the total amounts of such pollu-
tants emitted from stationary and mobile sources in the
United States (as contained in NEDS):
Particulates: 1.22%
S02: 0.537%
NOX: 0.00707%
Hydrocarbons: 0.664%
Carbon monoxide: 0.0516%
-------
SECTION 2
OVERVIEW MATRIX FOR NATIONAL CRITERIA POLLUTANT EMISSIONS
Data from NEDS and the following reference sources are included
in the data base which was used to generate the overview matrix:
Journals
Chemical Abstracts
Chemical and Engineering News
Chemical and Process
Engineering
Chemical Engineering
Chemical Engineering Progress
Chemical Engineering Science
Chemical Marketing Reporter
Chemical Technology
Chemical Week
Engineering Index
Environment
Environmental Science and
Technology
Hydrocarbon Processing
Books, Manuals, Reports
Industrial and Engineering
Chemistry
Journal of the Air Pollution
Control Association
Journal of the American
Chemical Society
Journal of the Chemical
Society (London)
Journal of Organic Chemistry
Journal of Physical Chemistry
Journal of the Water Pollution
Control Association
Modern Physics
Oil and Gas Journal
Pollution Abstracts
Air Pollution Engineering Manual, Second Edition, J. A. Danielson,
ed. Publication No. AP-40, U.S. Environmental Protection Agency,
Research Triangle Park, North Carolina, May 1973. 987 pp.
Chemical Engineer's Handbook, Fifth Edition. J. H. Perry and
C. H. Chilton, eds. McGraw-Hill Book Company, New York, New
York, 1973.
Compilation of Air Pollutant Emission Factors. Publication No.
AP-42, U.S. Environmental Protection Agency, Research Triangle
Park, North Carolina, March 1975.
Pervier, J. W., R. C. Barley, et al. Survey Reports on Atmos-
pheric Emissions from the Petrochemical Industry, Volumes I-IV.
EPA-450/3-73-005a-d, U.S. Environmental Protection Agency,
Research Triangle Park, North Carolina, April 1974.
-------
Kirk-Othmer Encyclopedia of Chemical Technology, Second Edition,
Volumes 1-22. John Wiley & Sons, Inc., New York, New York, 1969,
-------
OVERVIEW MATRIX FOR AIR POLLUTION SOURCES
SOURCE
MASS OF EMISSIONS (1000 KG/YRI
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
ABRASIVE PRODUCTS
ABRASIVE CLEANING OF OUTDOOR STRUCTURES
ACETALDEHYDE - HYDRATION OF ETHYLENE
ACETALOEHYDE - OXIDATION OF ETHANOL
ACETIC ACID
ACETIC ANHYDRIDE
ACETIC ACID . FROM HETHANOL
ACETIC ACID - FROfl BUTANE
ACETONE AND PHENOL FROM CUNENE
ACETONE • FROM ISOPROPANOL
ACETONE CYANOHYORIN
ACETYLENE
2560.0
0.00206
0.01440
8092. 0
0.00606
0.04510
0.0
0.00000
0.00000
0.0
0.00000
p. ooooo
0.0
0.00000
0.00000
4.0
0.00000
0.00002
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
o.o
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0,00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
o.poooo
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
5.2
0.00005
0.00002
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
736.2
0.00697
0.00330
0.0
0.00000
0.00000
19490.0
0.16800
0.07720
0.0
0.00000
0.00000
2980.0
0.02560
0.01180
8029.0
0.06910
0.03180
1293.0
0.01110
0.00512
2936.0
0.02530
0.01160
5313.0
0.04570
0.02100
2813.0
0.02420
0.01110
136.1
0.00117
0.00054
351.5
0.00303
0.00139
0.0
0.00000
0.00000
0.0
0.00000
0.00000
327.5
0.00037
0.00034
613.5
0.00069
0.00663
14230.0
0.01600
0.01460
0.0
0.00000
0.00000
916.1
0.00103
0.00094
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
MASS OF EMISSIONS (1000 KG/YRI
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
SOURCE
ACETYL CHLORIDE
ACROLEIN
ACRYLONITRILE
ACRYLIC ACID
ACRYLONITRILE - BUTADIENE - STYRENE RESIN
ADIPIC ACID
AOIPONITRILE
AEROSOL PROPELLANTS
AGRICULTURAL OPEN BURNING
AGRICULTURAL TILLING
ALACHLOR
ALCOHOL SULFATES - AMMONIUM SALT
ALCOHOL SULFATE - SODIUM SALT
PART
OiO
0.00000
0.00000
0.0
0,00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
S33.2
0.00042
0.00297
0.0
0.00000
0.00000
115000.0
0.09170
0.64000
S500000.0
4,39000
21.30000
0.0
0.00000
0.00000
0.4
0.00000
0.00000
0.7
0.00000
0.00000
S02
0.0
0.00000
0.00000
0.0
0.00000
0.00000
15.0
0.00007
0.00005
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0,00000
0.00000
0.0
0.00000
0.00000
0.9
0.00000
0.00000
1.7
0.00001
0.00001
NOX
0.0
0.00000
0.00000
0.0
0.00000
0.00000
473.0
0.00447
0.00212
76.6
0.00072
0.00034
0.0
0.00000
0.00000
3554.0
0.03360
0.01990
0.0
0.00000
0.00000
"
13520.0
0.12600
0.06050
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0,00000
0.00000
HC
1S.1
0.00016
0.00007
1665.0
0.01610
0.00739
56090.0
0.46300
0.22200
65.8
0,00057
0.00026
4.7
0.00004
0.00002
0.0
0,00000
0,00000
4715.0
0.04060
0.01870
--
135200.0
1.16000
0.53600
0.3
0.00000
0,00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
CO
»»
0.0
0.00000
0.00000
1640.0
0.00206
0.00189
66200.0
0.07650
0.07010
76.6
0.00009
o.ooooa
0.0
0.00000
0.00000
0.0
0,00000
0.00000
0.0
0,00000
0.00000
—
676200.0
0.75600
0.69500
0.0
0.00000
o.ooooo
0.0
0.00000
0.00000
0.0
0.00000
0.00000
c
2
2
2
2
2
2
2
2
1
4
2
2
2
-------
MASS OF EMISSIONS (1000 K6/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSIN6
00
SOURCE
ALCOHOL SULFATES - TRIETHANOLAMINE SALT
ALOICARB
ALKALI AND CHLORINE PLANT WASTES
ALKYD RESINS
ALLTL CHLORIDE
ALLYL ALCOHOL
ALUMINUM SULFATE
ALUMINUM CHLORIDE • ANHYDROUS
ALUMINUM HYDROXIDE
ALUMINUM FLUORIDE
ALUMINUM OXIpE - ALUMINA
AHINO RESINS
AMMONIA
PART
S02
NOX
HC
CO
0,3
0.00000
0.00000
1.1
0.00000
0.00001
0.7
0.00000
0.00000
464.9
0.00202
0.00154
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
3.4
0.00003
0.00001
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0,00000
0.00000
0.0
0.00000
b. ooooo
0.0
0.00000
0.00000
1204.0
0.00096
0.00671
30.3
0.00002
0.00017
460.2
0.00036
0.00267
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0,00000
0.00000
407.6
0.003S1
0.00162
7.1
0.00006
0.00003
2.7
0.00002
0.00001
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0,00000
0.0
0.00000
0.00000
0,0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0,0
0.00000
o.ooooo
2
2
2.
3
3
3
96260.0
0.04490
0.31300
S79.1
0.00046
0.00323
2046.0
0.00163
0.01140
0.0
0.00000
0.00000
772.2
0.00336
0,00256
3336.0
0.01450
0,01110
0.0
0,00000
0,00000
772.2
0.00729
0.00345
43990.0
0.41600
0.19700
0.0
0.00000
0.00000
1944.0
0.01330
0.00612
16690.0
0.14400
0.06610
0,0
0.00000
0.00000
0.0
0.00000
o.ooooo
14410.0
0.01620
0.01460
-------
SOURCE
MASS OF EMISSIONS (1000 K6/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
VO
AMMONIUM NITRATE
AMMONIUM PHOSPHATES
AMMONIUM ACETATE
AMMONIUM BENZOATC
AMMONIUM CITRATE
AMMONIUM FORMATE
AMMONIUM 6LUTONATE
AMMONIUM OXALATE
AMMONIUM TARTRATE
AMMONIUM THIOCYANATE
AMMONIUM SULFATE
AMYL ACETATE
ANILINE
18870.0
0.01510
0.10SOO
10230.0
0.00816
0.05700
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
10960.0
0.00875
0.06110
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
2.7
0.00002
0.00001
0.0
0.00000
0.00000
0.9
0.00000
0.00000
0.4
0.00000
0.00000
0.1
0.00000
0.00000
0.5
0.00000
0.00000
0.2
0.00000
0.00000
0.3
0.00000
0.00000
0.0
0.00000
0.00000
0.5
0.00000
0.00000
97.9
0.00084
0.00039
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
o.ooooo
0.00000
0.0
0.00000
o.ooooo
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
o.ooooo
0.00000
0.0
0.00000
0.00000
-------
SOURCE
MASS OF EMISSIONS (1000 K6XYR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
ANTHELMINTICS
ANTIMONY OXIDE
ARSENIC TRIOXIOE
ARTIFICIAL RIPENING OF FRUITS AND VEGETABLES
ASBESTOS PRODUCTS
ASBESTOS PROCESSING AREA
ASCORBIC ACID • VITAMIN C
ASPHALT ROOFING
ASPHALT PAVING - HOT NIX
ASPHALT PAVING - ORYER DRUM PROCESS
ASPIRIN
ATRA2INE
AUTOBODY INCINERATION
0.0
0.00000
0.00000
0.8
0.00000
0.00000
9.1
0.00001
0.00009
0.0
0.00000
0.00000
466. 1
0.00039
0.00271
31.5
0.00003
0.00016
0.0
0.00000
0.00000
23110.0
0.01640
0.12900
40290.0
0.03210
0.22400
1361.0
0.00109
0.00758
0.0
0.00000
0.00000
0.0
0.00000
0.00000
260.4
0.00021
0.00145
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0,00000
9551. 0
0.04160
0.03170
290.3
0.00126
0.00096
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
5372.0
0.05070
0.02400
163.3
0.00154
0.00073
0.0
0.00000
0.00000
0.0
0.00000
0.00000
13.0
0.00012
0.00006
6.8
0.00008
0.00003
0.0
0.00000
0.00000
0.0
0.00000
0.00000
544.3
0.00469
0.00216
0.0
0.00000
0.00000
10.5
0.00009
0.00004
6410.0
0.05520
0.02540
7167,0
0.06170
0.02840
254.1
0.00219
0.00101
29.5
0.00025
0.00012
74.8
0.00064
0.00030
65.1
0.00056
0.00026
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
3637.0
0.00430
0.00394
5671.0
0.00636
0.00563
172.4
0.00019
0.00016
0.0
0.00000
0.00000
0.0
0.00000
0.00000
325.5
0.00036
0.00033
-------
SOURCE
MASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSINS
PART
S02
NOX
HC
CO
AZINOPHOS - ETHYL
AZINOPHOS - METHYL
BACILLUS THURINGIENSIS
BARITE MILLING
BARITE TRANSPORT
BARITE STORAGE
BARIUM CHEHS • CARBONATE,CHLORIDE,HYDROXIDE,SULFATE.SULFIOE
BEEF CATTLE FEEOLOTS
BENEFIN
BENZENE
BENZOIC ACID
BENZONITRILE
BENZOYL CHLORIDE
0.7
0.00000
0.00000
0.9
0.00000
0.00001
0.5
0.00000
0.00000
3667.0
0.00293
0.01640
15.0
0.00001
0.00007
22.4
0.00002
0.00011
907.2
0.00072
0.00509
204400.0
0.16300
1.14000
1.3
0.00000
0.00001
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.2
0.00000
0.00000
0.3
0.00000
0.00000
0.0
0.00000
0.00000
7256.0
0.03160
0.02410
1.7
0.00001
0.00001
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1.4
0.00001
0.00000
0.2
0.00000
0.00000
0.2
0.00000
0.00000
0.0
0.00000
0.00000
134.3
0.00127
0.00060
1.3
0.00001
0.00001
10770.0
0.10200
0.04620
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1.0
0.00001
0.00000
1.4
0.00001
0.00001
0.0
0.00000
0.00000
105.2
0.00091
0.00042
0.0
0.00000
0.00000
5126.0
0.04410
0.02030
210.7
0.001S1
0.00063
0.3
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
616.9
0.00069
0.00063
0.0
0.00000
o.ooooo
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
MASS OF EMISSIONS (1000 KG/YRI
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
SOURCE
BENZYL CHLORIDE
BERYLLIUM COMPOUNDS
BISPHENOL-A
BLASTING OF SULFUR STORAGE PILES
BORIC ACID AND BORAX • SODIUM TETRABORATE
BRAKE SHOE DEBONDIN6
BRASS AND BRONZE INGOT PRODUCTION
BREAKING AND SCUTCHING FLAX FIBRES
BRICK AND TILE KILNS AND DRYERS
BROMACXl.
BROMINE
BRUCINE ALKALOID
BUILDING DEMOLITION
PART
0.0
0.00000
0.00000
47690.0
0.03620
0.26700
S02
0.0
0.00000
0,00000
NOX
0.0
0.00000
0.00000
HC
0.0
0.00000
0.00000
CO
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
34040.0
0.02720
0.14900
2177.0
0.00174
0.01210
6.1
0.00000
0.00003
1372.0
0.00109
0.00764
21.4
0.00002
0.00012
2336.0
0.00186
0.01300
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
2.2
0.00001
0.00001
0.0
0.00000
0.00000
0.0
0.00000
0.00000
141700.0
0.61600
0.47000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.2
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
8660.0
0.06200
0.03660
0.0
0.00000
0.00000
72.6
0.00063
0.00029
0.0
0.00000
0,00000
299.7
0.00255
0.00117
0.0
0.00000
0.00000
0.4
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
9734.0
0.08380
0.03660
2.7
0.00002
0.00001
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
4.9
0.00001
0.00001
0.0
0.00000
0,00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
SOURCE
MASS OF EMISSIONS (1000 KG/TR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
U>
BUTACHLOR
BUTADIENE
2-BUTOXYETHANOL
S-BUTYL ALCOHOL
BUTYLCNE DINER - DIISOBUTYLENE
N-BUTYL ACRYLATE
BUTYL RUBBER
BUTYL OCTYL PHTHALATE
T-BUTYL ALCOHOL
BUTYLAMINE
N-BUTYL ACETATE
N-BUTYL ALCOHOL
BUTYLATE
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1.8
0.00000
0.00001
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
743.9
0.00324
0.00247
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
6.6
0.00006
o.oooos
20930.0
o.ieooo
0.08290
37.8
0.00032
0.00015
1502.0
0.01290
0.00595
10.2
0.00009
0.00004
72.6
0.00062
0.00029
1037.0
0.00893
0.00411
5.4
o.oooos
0.00002
21.8
0.00019
0.00009
4.1
0.00004
0.00002
38.8
0.00033
0.00015
569.8
0.00490
0.00226
5.4
O.OOOOS
0.00002
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
17320.0
0.01940
0.01780
0.0
0.00000
0.00000
-------
SOURCE
MASS OF EMISSIONS (1000 KS/TR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
N-BUTYRALOEHYOE
N-BUTYRIC ACID
CACOOYLIC ACID
CADMIUM PIGMENTS - CADMIUM SULFIOE. SULFOSELENIDE. LITHOPONE
CALCIUM ACID HETHANEARSONATE
CALCIUM CARBONATE
CALCIUM CHLORIDE
CALCIUM CARBIDE
CALCIUM ARSENATE
CALCIUM PHOSPHATE
CAPROLACTAM
CAPTAN
CAPTAFOL
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
37.1
0.00003
0.00021
607.4
0.00061
0.00<«50
0.0
0.00000
0.00000
0.6
0.00000
0.00000
0.1
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0,00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
614.4
0.00701
0.00323
0.5
0.00000
0.00000
1.5
0.00001
0.00001
0.0
0.00000
0.00000
0.0
0.00000
0.00000
159.1
0.00134
0.00061
9.1
o.ooooe
0.00004
1.4
0.00001
0.00001
1629.0
0.00163
0.00167
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
300.5
0.00024
0.00167
6692.0
0.00550
0.03640
12160.0
0.00970
0.06760
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1106.0
0.00461
0.00367
0.0
0.00000
0.00000
0.0
0,00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0,00000
0.0
0.00000
0.00000
0.0
0.00000
0,00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0,0
0.00000
0.00000
-------
U1
SOURCE
CARBARYL
CARBON BLACK - FURNACE
CARBONIZING yOOL FIBRES
CARBON BLACK - THERMAL
CARBON TETRACHLORIOE - METHANE
CARBON TETRACHLORIOE - CHLORINATION OF PROPANE
CARBON DISULFIOE
CARBOFURAN
CARBON TETRACHLORIOE - CARBON DISULFIOE
CARDING ASBESTOS FIBRES
CARDING OF COTTON FIBRES
CARDING WOOL FIBRES
CARPET DYEING AND DRYING COTTON
MASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
13.1
0.00001
0.00007
1011.0
0.00081
O.OOS63
0.0
0.00000
0.00000
342.1
0.00149
0.00114
0.0
0.00000
0.00000
1339.0
0.01260
O.OOS99
39.9
0.00034
0.00016
70200.0
0.60400
0.27800
0.0
0.00000
0.00000
2082000.0
2.33000
2.14000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
111.0
0.00009
0.00062
2.3
0.00000
0.00001
0.0
0.00000
0,00000
27. 5
0.00002
0.00015
1406.0
0.00112
0.00784
1793.0
0.00143
0.00998
0.0
0.00000
0.00000
10.9
O.OOOOS
0.00004
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1659.0
0.00722
0.00551
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
28.5
0.00027
0.00013
0.0
0.00000
0.00000
0.0
0.00000
0.00000
48.6
0.00046
0.00022
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
7966.0
0.06860
0.03160
4128.0
0.03550
0.01640
55.5
0.00048
0.00022
6.8
0.00006
0.00003
4253.0
0.03660
0.01690
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.9
0.00001
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
o.ooooo
0.00000
0.0
o.ooooo
0.00000
0.0
o.ooooo
o.ooooo
0.0
o.ooooo
o.ooooo
0.0
0.00000
0.00000
0.0
o.ooooo
o.ooooo
0.0
0.00000
0.00000
-------
SOURCE
MASS OF EMISSIONS 11000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC-
CO
CARPET BACKING - COTTON
CARPET BACKING - FLAX
CARPET DYEIN6 AND DRYIN6 FLAX
CARPET DYEING AND DRYING NATURAL POLYMER FABRICS
CARPET DYEING AND DRYING RAYON FABRICS
CARPET DYEING AND DRYING WOOL
CARPET BACKING SYNTHETIC POLYMERS
CARPET DYEING AND DRYING SYNTHETIC POLYMERS
CATECHOL
CDEC
CELLULOSE ACETATE
CEMENT
CHARCOAL MANUFACTURE
0.7
0.00000
0.00000
i.e
0.00000
0.00001
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
62.9
o.oooos
0.00035
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.2
0.00000
0.00000
0.0
0.00000
0.00000
878000.0
0.70000
4.89000
17690.0
0.01410
0.09850
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
74. 4
0.00032
0.00025
0.0
0.00000
0.00000
741000.0
3.22000
2.16000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0,00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
91310.0
0.86200
0.40800
32430.0
0.30600
0.14500
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1.0
0.00001
0.00000
i.e
0.00002
0.00001
9.1
0.00008
0.00004
12.9
0.00011
0.00005
0.0
0.00000
0.00000
271.2
0.00233
0.00107
1.1
0.00001
0.00000
0.5
0.00000
0.00000
1898.0
0.01630
0.00752
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
38330.0
0.04300
0.03940
-------
MASS OF EMISSIONS (1000 K6/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
SOURCE
CHLOROFORM
CHLOROBENZENE
CHLOROACETIC ACID
CHLOROPHENOL
CHLOROANE
CHLOROSULFONIC ACID
CHLOROTRIFLUORO METHANE
CHLORAMBEN
CHLORPYRIFOS
CHLOROSULFONIC ACID - INORGANIC ACIDS
CHLORINATION OF SWIMMING POOLS
CHOLINE CHLORIDE
CHROMIUM COMPOUNDS - ACETATE, BORIDES, HALIDES. ETC.
PART
1.1
0.00000
0.00001
S02
464.9
0.00202
0.00154
NOX
0.0
0.00000
0.00000
HC
0.0
0.00000
0.00000
CO
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0,00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
2150.0
o.oiaso
0.00852
101.9
o.oooea
0.00040
45.7
0.00039
0.00018
12.7
0.00011
0.00003
6.8
0.00006
0.00003
70.5
0.00061
0.00028
5.4
0.00005
0.00002
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.1
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
31.6
0.00027
0.00012
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
SOURCE
CHROMIUM OXIDE - INORGANIC PIGMENT
CHRONIC ACID
CLAY PROCESSING AREA
CLAY SILOS - KAOLIN
COAL REFUSE PILESt OUTCROPS AND ABANDONED MINES
00
COAL CLEANING PLANTS - THERMAL DRYING
COAL CLEANING PLANTS - PNEUMATIC
COAL TRANSPORT
COAL ASH DISPOSAL
COAL CONVEYING
COAL STORAGE
COAL FINES DISPOSAL
COBALT COMPOUNDS - ACETATE. CARBONATE. HALIDES. ETC.
MASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
0.3
0.00000
0.00000
1.2
0.00000
0.00001
39050.0
0.03120
0.13400
5297.0
0.00i»23
0.02650
99730.0
0.07960
0.55600
7244.0
0.00578
0.04040
922.6
0.00074
0.00514
32560.0
0.02600
0.18100
639.8
0.00051
0.00354
2505.0
0.00200
0.01400
497.8
0.00040
0.00251
80150.0
0.06390
0.34000
8.5
0.00001
0.00005
5.6
0.00002
0.00002
0.0
0.00000
0.00000
183600.0
0.79900
0.60900
241.5
0.00105
0.00080
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
30590.0
0.28900
0.13700
2415.0
0.02280
0.01080
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
61180.0
0.52700
0.24200
2415.0
0.02080
0.00957
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
305900.0
0.34300
0.31400
2415.0
0.00271
0.00248
0.0
0.00000
0.00000
0.0
0.00000
0.00000
3
3
4
4
1
3
3
4
4
4
4
4
3
-------
SOURCE
MASS OF EMISSIONS (1000 K6/TR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
COFFEE ROASTING
COKE MANUFACTURE
COMBING ASBESTOS FIBRES
COMBING OF COTTON FIBRES
COMBING FLAX FIBRES
COMBING WOOL FIBRES
COMMERCIAL/INSTITUTIONAL EXT COMB BITUMINOUS PULV DRY BOTH
COMMERCIAL/INSTITUTIONAL EXT COMB BITUMINOUS PULV WET BOTH
COMMERCIAL/INSTITUTIONAL EXT COMB BITUMINOUS STOKER
COMMERCIAL/INSTITUTIONAL EXT COMB ANTHRACITE STOKER
COMMERCIAL/INSTITUTIONAL EXT COMB RESIO OIL TANG FIRE
COMMERCIAL/INSTITUTIONAL EXT COMB RESID OIL OTHER
COMMERCIAL/INSTITUTIONAL EXT COMB DIST OIL TANG FIRE
6002.0
0.00479
0.03340
218200.0
0.17400
1.22000
27.5
0.00002
0.00015
172.3
0.00014
0.00096
3.6
0.00000
0.00002
1403.0
0.00112
0.007S1
544.8
0.00043
0.00303
4058.0
0.00324
0.02260
45320.0
0.03620
0.25200
19060.0
0.01520
0.10600
661.5
0.00053
0.00368
82680.0
0.06600
0.46100
535.8
0.00043
0.00298
0.0
0.00000
0.00000
161700.0
0.70400
0.53700
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
38090.0
0.16600
0.12600
1777.0
0.00774
0.00590
154200.0
0.67100
0.51200
18110.0
0.07880
0.06010
8603.0
0.03740
0.02860
1090000.0
4.74000
3.62000
1179.0
0.00513
0.00392
0.0
0.00000
0.00000
1581.0
0.01490
0.00707
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
2540.0
0.02400
0.01140
118.5
0.00112
0.00053
9986.0
0.09430
0.04470
14560.0
0.13800
0.06510
1180.0
0.01110
0.00528
290300.0
2.74000
1.30000
1453.0
0.01370
0.00650
16660.0
0.14300
0.06600
167600.0
1.44000
0.66400
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1180.0
0.01020
0.00467
56.8
0.00049
0.00022
4904.0
0.04220
0.01940
190.6
0.00164
0.00075
86.0
0.00074
0.00034
10900.0
0.09380
0.04320
109.0
0.00094
0.00043
0.0
0.00000
0.00000
50200.0
0.05630
0.05160
0.0
0.00000
0.00000
0.0
o.ooooo
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
4176.0
0.00468
0.00429
19.4
0.00002
0.00002
16350.0
0.01830
0.01680
1906.0
0.00214
0.00196
118.0
0.00013
0.00012
14500.0
0.01630
0.01490
145.3
0.00016
0.00015
-------
SOURCE
MASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
NJ
O
COMMERCIAL/INSTITUTIONAL EXT cone DIST OIL OTHER
COMMERCIAL/INSTITUTIONAL EXT cone CAS TANG FIRE
COMMERCIAL/INSTITUTIONAL EXT COMB SAS OTHER
COMMERCIAL/INSTITUTIONAL INT COMB OlST OIL
COMMERCIAL/INSTITUTIONAL INT CONB SAS
CONSTRUCTION ACTIVITIES
CONVERSION OF CRUDE IODINE TO RESUBLIHEO AND IODINE PRODUCTS
CONVEYING OF SAND AND GRAVEL
COPPER SULFATE - PENTAHYDRATE
COTTONSEED OIL HILLING
COTTON GINS
COTTON HARVESTING
COVERED WIRE INCINERATION
52670.0
0.04200
0.29300
353.9
0.00026
0.00197
7892.0
0.00630
0.04400
1784.0
0.00142
0.00994
0.0
0.00000
0.00000
3414000.0
2.72000
19.00000
117900.0
0.51300
0.39100
21. B
0.00009
0.00007
490.1
0.00213
0.00163
2292.0
0.00998
0.00761
0.6
0.00000
0.00000
281100.0
2.66000
1.26000
4262.0
0.04020
0.01910
95060.0
0.89800
0.42500
21250.0
0.20100
0.09510
6807.0
0.06430
0.03050
10880.0
0.09370
0.04310
281.2
0.00242
0.00111
6261.0
0.05390
0.02480
1442.0
0.01240
0.00571
0.0
0.00000
0,00000
14510.0
0.01630
0.01490
734.4
0.00082
0.00075
16310.0
0.01830
0.01660
3826.0
0.00429
0.00393
0.0
0.00000
0.00000
1
1
1
1
1
4
4171.0
0.00333
0.01600
34.5
0.00003
0.00019
6164.0
0.00492
0.03430
7254.0
0,00579
0,04040
221.6
0.00018
0.00123
1089.0
0.00087
0.00606
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
54.4
0.00051
0.00024
0.0
0.00000
0.00000
10270.0
0,08840
0.04070
0.0
0.00000
0.00000
272.2
0.00234
0.00108
0.0
0.00000
o.obooo
0.0
0.00000
o.ooooo
0.0
0.00000
0.00000
1361.0
0.00133
0.00140
-------
SOURCE
MASS OF EMISSIONS (1000 K6/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
F1-CRESOL
CRESOL - SYNTHETIC
CRESYLIC ACID
CRESYLDIPHENYL PHOSPHATE
CROTONALDEHYDE
to CRUDE IODINE - DOHESTIC PRODUCTION
H
CRUSHED SANDSTONE
CRUSHED GRANITE
CRUSHED STONE/TRAPROCK
CRUSHED LIMESTONE
CRUSHING, SIZING OF SAND AND GRAVEL
CUHENE
CUHENE SULFONATE - AHHONIUM SALT
0.0
0.00000
0.00000
131.3
0.00010
0.00073
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
838.8
0.00067
0.00467
10580.0
0.008<»t
0.09890
3051.0
0.00243
0.01700
2137.0
0.00170
0.01190
37540.0
0.03000
0.14400
573.8
0.00046
0.00320
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
22.0
0.00021
0.00010
109.4
0.00103
0.00049
255.3
0.00241
0.00114
0.0
0.00000
0.00000
0.0
0.00000
0.00000
10.5
0.00009
0.00004
1094.0
0.00942
0.00433
121.6
0.00105
0.00048
3.3
0.00003
0.00001
4.9
0.00004
0.00002
0.0
0.00000
0.00000
350.0
0.00039
0.00036
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1721.0
0.01480
0.00682
4.5
0.00004
0.00002
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
SOURCE
MASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
CUHENE SULFONIC ACID
CTCLOHEXANONE
CYCLOHEXYLAHINE
1< 5-CYCLOOCTADIENE
CTCLOHEXANE
C4 HYDROCARBONS
C5 HYDROCARBONS
2.4-D ACID. ESTERS, SALTS
OALAPON
DBCP
DDT
DECYL ALCOHOL
DEEP FRYING
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
24.9
0.00002
0.00014
t.l
0.00000
0.00001
0.0
0.00000
0.00000
13.6
0.00001
0.00008
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
T75.2
0.00337
0.00257
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
10450.0
0.09870
0.04670
1210.0
0.01140
0.00541
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
4.4
0.00004
0.00002
31240.0
0.26900
0.12400
3.7
0.00003
0.00001
13.6
0.00012
0.00005
7752.0
0.06670
0.03070
4976.0
0.04280
0.01970
576.2
0.00496
0.00228
24.9
0.00021
0.00010
1.1
0.00001
0.00000
9.1
0.00008
0.00004
27.2
0.00023
0.00011
71.1
0.00061
0.00028
14970.0
0.12900
0.05930
0.0
0.00000
0.00000
34380.0
0.03880
0.03550
0.0
0.00000
o.oooob
0.0
0.00000
0.00000
9691.0
0.01090
0.00996
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
o.ooooo
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
106.7
0.00012
0.00011
0.0
0.00000
0.00000
2
2
2
2
2
2
2
2
2
2
2
2
2
-------
MASS OF EMISSIONS (1000 KG/TRI
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
to
CO
SOURCE
DEFOLIATION OF COTTON
DI BUTYL PHTHALATE
DI-B-ETHYLHEXYL PHTHALATE
DI-2-ETHYLHEXYL AOIPATE
DIAZINON
DICAMBA
0-DICHLOROBENZENE
P'DICHLOROBENZENE
OICHLOROBENZONITRILE
DICHLOROOIFLUOROHETHANE
OICHLORONAPHTHO QUINONC
DICHLOROTETRAFLUOROETHANE
OICHLOROVOS
PART
S02
NOX
HC
CO
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
2.7
0.00000
0.00002
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.2
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1116.0
0.001*66
0.00370
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
o.ooodo
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
19.7
0.00017
o.ooooa
641.3
0.00992
0.0025"*
10.2
0.00009
O.OOOOl*
0.0
0.00000
0.00000
2.7
0.00002
0.00001
640.1
0.00391
0.00254
947.1
0.00815
0.00375
0.0
0.00000
0.00000
649.1
0.00731
0.00336
4.9
0.00004
0.00002
19.1
0.00013
0.00006
0.4
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
SOURCE
MASS OF EMISSIONS (1000 K6/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
DICHLOROPROPENE
OICOFOL
DICROTOPHOS
DIETHYLAMINE
OIISODECYL PHTHALATE
DIISOOCTAL PHTHALATE
DIMETHYL PHTHALATE
DIMETHYL TEREPHTHALATE
DIMETHYL HYDRAZINE
OIMETHOATE
DINITROTOLUENE
DINITROBENZENE
DINITROPHENOL
0.0
0.00000
0.00000
0.9
0.00000
0.00001
0.2
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
734.9
0.00059
0.00409
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
962.9
0.00245
0.00167
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
46.9
0.00044
0.00021
11.3
0.00010
0.00004
i.a
0.00002
0.00001
0.2
0.00000
0.00000
5.0
0.00004
0.00002
154.9
0.00133
0.00061
39.4
0.00034
0.00016
10.0
0.00009
0.00004
49440.0
0.42600
0.19600
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
28710.0
0.03220
0.02950
0.7
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.4
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.4
0.00000
0.00000
4.0
0.00004
0.00002
0.0
0.00000
0.00000
0.2
0.00000
0.00000
2.7
0.00002
0.00001
14.7
0.00013
0.00006
1.4
0.00001
0.00001
0.7
0.00001
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
SOURCE
Ul
DINOSEB
DIOUAT
DISPOSAL OP CONCRETE BLOCK WASTES
DISPOSAL OF ASBESTOS WASTE ORE
DISTILLED LIQUOR
DISULFOTON
DIURON
DOOECYLBENZENE SULFONIC ACID
DODECYLBENZENE SULFONIC ACID - SODIUH SALT
DOOECYLBENZENE SULFONIC ACID - TRIETHYLAFIINE SALT
DODECYLBENZENE - HARD
OOOECENE - NON-LINEAR
DODECYLBENZENE SULFONIC ACID - CALCIUM SALT
NASS OF EMISSIONS (1000 K6/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
1.3
0.00000
0.00001
0.0
0.00000
0.00000
2996.0
0.00239
0.01670
7620.0
0.00600
0.04240
2640.0
0.00211
0.01470
2.3
0.00000
0.00001
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1.7
0.00001
0.00001
0.0
0.00000
0.00000
0.0
0.00000
0.00000
929.9
0.0040S
0.00309
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1.3
0.00001
0.00001
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1.4
0.00001
0.00001
0.3
0.00000
0.00000
10560.0
0.09090
0.04160
0.0
0.00000
0.00000
2.3
0.00002
0.00001
664.8
0.00572
0.00263
1694.0
0.01460
0.00671
31.3
0.00027
0.00012
561.3
0.004S3
0.00222
105.2
0.00091
0.00042
56.3
0.0004B
0.00022
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
280.7
0.00031
0.00029
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
SOURCE
DOOECYLBENZENE SULFONIC ACID - ISOPROPYLEHINE SALT
DRAWING AND SPINNING COTTON FIBRES
DRAWING AND SPINNING FLAX FIBRES
DRAWING AND SPINNING WOOL FIBRES
DRILLING OIL AND GAS - BEFORE WELL HIT
to
(Tv
DRUM INCINERATION
OSHA
DYEING COTTON FABRICS
DYEING LINEN FABRICS
DYEING NATURAL POLYMER FABRICS
DYEING RAYON FABRICS
DYEING SILK FABRICS
DYEING AND DRYING WOOL FIBRE STOCK
MASS OF EMISSIONS 11000 K6/TR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
0.0
0.00000
0.00000
5071.0
0.00*05
0.02820
5.3
0.00000
0.00003
135.1
0.00011
0.00075
62.1
0.00005
0.00024
<»76.3
0.00030
0.00265
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
66.7
0.00063
0.00030
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
10.0
0.00009
0.00001
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
285.6
0.00216
0.00113
3.0
0.00001
0.00002
1611.0
0.03970
0.01830
0.1
0.00000
0.00000
0.7
0.00001
0.00000
2.7
0.00002
0.00001
0.0
0.00000
0.00000
0.1
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
790.6
0.00089
0.00081
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
o.ooooo
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
SOURCE
DYEING WOOL FABRICS
DYEING SYNTHETIC POLYMER FABRICS
ELECTRICAL EQUIPMENT WINDING RECLAMATION
ELECTRICITY GENERATION EXT COMB BITUMINOUS PULV WET BOTH
ELECTRICITY GENERATION EXT COMB BITUMINOUS CYCLONE
ELECTRICITY GENERATION EXT COMB BITUMINOUS STOKER
ELECTRICITY GENERATION EXT COMB ANTHRACITE PULV DRY BOTH
ELECTRICITY GENERATION EXT COMB ANTHRACITE STOKER
ELECTRICITY GENERATION EXT COMB LIGNITE PULV DRY BOTH
ELECTRICITY GENERATION EXT COMB LIGNITE PULV UET BOTH
ELECTRICITY GENERATION EXT COMB LIGNITE CYCLONE
ELECTRICITY GENERATION EXT COMB LIGNITE STOKER
ELECTRICITY GENERATION EXT COMB RESIO OIL TANG FIRE
MASS OF EMISSIONS (1000 K6/YRI
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
0.0
0.00000
0.00000
0.0
0.00000
0.00000
312.5
0.00029
0.00174
453700.0
0.36200
2.53000
226900.0
0.18100
1.26000
66740.0
0.05480
0.38300
15430.0
0.01230
0.08590
3447.0
0.00275
0.01920
45250.0
0.03610
0.25200
11770.0
0.00939
0.06560
7624.0
0.00608
0.04250
7598.0
0.00606
0.04230
42730.0
0.03410
0.23800
0.0
0.00000
0.00000
0.0
0.00000
0.00000
5.3
0.00002
0.00002
1724000.0
7.50000
5.72000
1724000.0
7.50000
5.72000
89650.0
0.39000
0.29800
13600.0
0.05920
0.04520
23570.0
0.10300
0.07820
67020.0
0.29200
0.22200
17230.0
0.07500
0.05720
10920.0
0.04750
0.03620
10890.0
0.04740
0.03610
526400.0
2.29000
1.75000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
182.7
0.00173
0.00082
688600.0
6,50000
3.08000
1270000.0
12.00000
5.68000
18070.0
0.17100
0.08080
4164.0
0.03930
0.01860
6421.0
0.06060
0.02870
38100.0
0.36000
0.17000
9039.0
0.08540
0.04040
3445.0
0.03250
0.01540
3447.0
0.03260
0.01540
163400.0
1.54000
0.73100
0.4
0.00000
0.00000
3842.0
0.03310
0.01520
14.9
0.00013
0.00006
6886.0
0.05930
0.02730
6886.0
0.05930
0.02730
1087.0
0.00935
0.00431
7.3
0.00006
0.00003
81.4
0.00070
0.00032
3358.0
0.02890
0.01330
903.9
0.00778
0.00358
571.4
0.00492
0.00226
572.7
0.00493
0.00227
3265.0
0.02810
0.01290
0.0
0.00000
0.00000
0.0
0.00000
0.00000
36.5
0.00004
0.00004
23460.0
0.02630
0.02410
23460.0
0.02630
0.02410
2391.0
0.00264
0.00241
23.6
0.00003
0.00002
861.6
0.00097
0.00068
3356.0
0.00376
0.00345
903.9
0.00101
0.00093
1177.0
0.00132
0.00121
1179.0
0.00132
0.00121
16340.0
0.01830
0.01680
-------
MASS OF EMISSIONS (1000 K6/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
to
00
SOURCE
ELECTRICITY GENERATION EXT COMB RESID OIL OTHER
ELECTRICITY GENERATION EXT COMB DIST OIL TANG FIRE
ELECTRICITY GENERATION EXT COMB DIST OIL OTHER
ELECTRICITY GENERATION EXT COMB GAS TANG FIRE
ELECTRICITY GENERATION EXT COMB GAS OTHER
ELECTRICITY GENERATION EXT COMB REFUSE
ELECTRICITY GENERATION INT COMB DIST OIL TURBINE
ELECTRICITY GENERATION INT COMB GAS TURBINE
ELECTRICITY GENERATION INT COMB DIST OIL RECIP ENG
ELECTRICITY GENERATION INT COMB GAS RECIP ENG
ELECTRICITY GENERATION EXT COMB BITUMINOUS PULV DRY BOTH
ELECTROLYTIC PRODUCTION OF CHLORINE
ENDOSULFAN
PART
66040.0
0.05270
0.36800
1361.0
0.00109
0.00756
2178.0
0.00174
0.01210
3548.0
0.00283
0.01980
10840.0
0.00865
0.06040
600100.0
0.47900
3.34000
4620.0
0.00369
0.02580
1453.0
0.00116
0.00809
19010.0
0.01520
0.10600
299.7
0.00024
0.00167
3174000.0
2.53000
17.70000
—
0.0
0.00000
0.00000
S02
816100.0
3.35000
2.71000
5542.0
0.02410
0.01B40
8705.0
0.03790
0.02890
208.7
0.00091
0.00069
653.4
0.00284
0.00217
18130.0
0.07890
0.06020
3268.0
0.01420
0.01080
526.3
0.00229
0.00175
2631.0
0.01140
0.00873
12.7
0.00006
0.00004
9073000.0
39.50000
30.10000
--
0.0
0.00000
0.00000
NOX
535300.0
5.06000
2.39000
8718.0
0.08230
0.03900
2903.0
0.02740
0.01300
108800.0
1.03000
0.48700
761800.0
7.19000
3.41000
1180.0
0.01110
0.00528
62570.0
0.59100
0.28000
41690.0
0.39400
0.18600
271100.0
2.56000
1.21000
108800.0
1.03000
0.48700
2175000.0
20.50000
9.73000
•»•
0.0
0.00000
0.00000
HC
4988.0
0.04290
0.01980
345.2
0.00297
0.00137
554.5
0.00477
0.00220
354.8
0.00305
0.00141
1084.0
0.00933
0.00429
0.0
0.00000
0.00000
5174.0
0.04450
0.02050
4268.0
0.03670
0.01690
21730.0
0.18700
0.08610
25.4
0.00022
0.00010
37240.0
0.32100
0.14800
--
1.4
0.00001
0.00001
CO
25400.0
0.02850
0.02610
526.6
0.00059
0.00054
817.9
0.00092
0.00084
5993.0
0.00672
0.00616
18560.0
0.02080
0.01910
333.6
0.00038
0.00034
14330.0
0.01630
0.01490
11840.0
0.01330
0.01220
56940.0
0.06380
0.05650
2456.0
0.00275
0.00252
127500.0
0.14300
0.13100
—
0.0
0.00000
0.00000
c
1
1
1
1
1
1
1
1
1
1
1
3
2
-------
SOURCE
MASS OF EMISSIONS (1000 K6/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
IO
ENORIN
EPICHLOROHYORIN
EPOXY RESINS - MODIFIED
EPOXY RESINS • UNMODIFIED
EPTC
ETHANOL
ETHANOLAMINE - MONO-.DI-«AND TRI
ETHOXYLATED NONYLPHENOL
ETHOXYLATED MIXED LINEAR ALCOHOLS
ETHOXYLATED OCTYLPHENOL
2-ETHOXYETHYL ACETATE
ETHOXYETHANOL
ETHYLENE OXIQE
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1.4
0.00000
0.00001
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
SS7.9
0.00243
0.00169
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1.4
0.00001
0.00001
406.2
0.00351
0.00162
82.6
0.00071
0.00033
144.0
0.00124
O.OOOS7
4.1
0.00004
0.00002
1902.0
0.01290
0.00999
1917.0
0.01310
0.00601
49.3
0.00042
0.00019
4.0
0.00003
0.00002
1.2
0.00001
0.00000
13.6
0.00012
o.oooos
30.8
0.00026
0.00012
84890.0
0.73000
0.33600
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0,00000
0.0
0.00000
0.00000
0.0
o.ooooo
0.00000
16.8
0.00002
0.00002
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
o.o
0.00000
0.00000
-------
SOURCE
ETHYL BENZENE
ETHYLENE SLYcOL
ETMYLENE
ETHYL CHLORIDE - ETHYLENE HYOROCHLORINATION
ETHYL ACRVLATE - DIRECT ESTERIFICATION
Ul
O
ETHYL ACRYLATE - CARBONYLATION OF ACETYLENE
ETHYL ACETATt
ETHYL ETHER
ETHYLENE - PROPYLENE TERPOLYMER
2-ETHYL-l-HEXANOL
ETHYLENE-PROPYLENE RUBBER
ETHYLENE OlAHlNE
ETHYL BUTYRATE
MASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOYAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
. 0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
24020.0
0.22700
0.10700
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
44660.0
0.38SOO
0.17700
2276.0
0.01960
0.00902
11440.0
0.09850
0.04530
5205.0
0.04460
0.02060
1207.0
0.01040
0.00476
1217.0
0.01050
0.00462
461.5
0.00397
0.00163
74.6
0.00064
0.00030
16570.0
0.14300
0.06570
41350.0
0.35600
0.16400
7926.0
0.06820
0.03140
36.7
0.00032
0.00015
0.3
0.00000
0.00000
9531.0
0.01070
0.00979
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1207.0
0.00135
0.00124
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
SOURCE
MASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
ETHYLENE DIBROMIDE
ETHYLENE OICHLORIDE - ETHYLENE CHLORINATION
ETHYLENE OICHLORIDE - OXYHYDROCHLORINATION
EXFOLIATED VERHICULITE
EXPLOSIVES BURNING
FELTING WOOL FABRICS
FENSULFOTHION
FERROALLOY PRODUCTION
FERTILIZER MIXING - AHHONIATION - GRANULATION PLANTS
FERTILIZER MIXING - LIQUID MIX PLANTS
FERTILIZERS . BULK BLENDING PLANTS
FINISHING COTTON FABRICS
FINISHING LINEN FABRICS
OtO
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1365.0
0.00109
0.00760
370.9
0.00030
0.00207
0.2
0.00000
0.00000
1.4
0.00000
0.00001
136300.0
0.11000
0.77100
1911.0
0.001S2
0.01060
iso. a
0.0001"*
0.00101
2200.0
' 0.00176
0.01230
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1071.0
0.001*66
0.00356
0.0
0.00000
0.00000
557.9
0.00243
0.00185
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
752.1
0.00710
0.00336
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
357.8
0.00308
0. 001*2
29820.0
0.25700
0.11800
21470.0
0.18500
0.06510
0.0
0.00000
0.00000
463.6
0.00399
0.00184
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
296.4
0.00255
0.00117
43.2
0.00037
0.00017
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
MASS OF EMISSIONS (1000 KS/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
SOURCE
FINISHING NATURAL POLYHER FABRICS
FINISHING RAYON FABRICS
FINISHING SILK FABRICS
FINISHING WOOL FABRICS
FINISHING SYNTHETIC POLYMER FABRICS
CO FISH AND SEAFOOD CANNING
FLAT GLASS* PRESSED AND BLOWN GLASS. AND GLASS CONTAINERS
FLUOHETURON
FLUORINE
FOLPET
FOOD PREPARATION
FORMALDEHYDE
FORniC ACID
PART
0.1
0.00000
0.00000
499.7
0.00040
0.00278
0.0
0.00000
0.00000
0.0
0.00000
0.00000
S02
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
NOX
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
HC
0.00001
0.00001
0.0
0.00000
0.00000
22500.0
0.19400
0.08910
14.9
0.00013
0.00006
CO
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
44030.0
0.03510
0.24500
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
34080.0
0.14800
0.11300
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
68160.0
0.64400
0.30500
0.0
0.00000
0.00000
564.4
0.00486
0.00224
2258.0
0.01940
0.00895
37.7
0.00032
0.00015
305.9
0.00263
0.00121
59.5
0.00051
0.00024
340.3
0.00293
0.00135
3408.0
0.02930
0.01350
1.1
0.00001
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
85.2
0.00010
0.00009
0.0
0.00000
0.00000
0.0
0.00000
0.00000
2998.0
0.00336
0.00308
0.0
0.00000
0.00000
223.5
0.00025
0.00023
-------
SOURCE
FRUIT AND VEGETABLE FREEZING
FRUIT AND VEGETABLE CANNING
FUHARIC ACID
GAS FIRED LAUNDRY DRYING
GAS FIRED AIR CONDITIONING
OJ
U)
GASOLINE DISTRIBUTION - AUTOMOBILE TANK LOADING
GASOLINE DISTRIBUTION • SERVICE STATION TANKS
GASOLINE DISTRIBUTION - TERMINAL LOADING AND STORAGE
GILLIN6 WOOL FIBRES
GLYCERIN - ACROLEIN
GLYCERIN TRIPOLYOXYPROPYLENE ETHER
GLYCERIN - ALLYL ALCOHOL
GLYCERIN - ALLYL CHLORIDE
MASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
426. B
0.00034
0.00238
517.6
0.00041
0.00288
0.0
0.00000
0.00000
817.0
0.0006S
0.00455
1826.0
.0.00146
0.01020
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
99.3
o.oooos
0.00033
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
25.8
0.00011
0.00009
57.7
0.00025
0.00019
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
853.7
0.00806
0.00382
1036.0
0.00978
0.00463
0.0
0.00000
0.00000
3225.0
0.03050
0.01440
7210.0
0.06810
0.03230
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
21340.0
0.18400
0.08460
25890.0
0.22300
0.10300
460.1
0.00396
0.00182
344.0
0.00296
0.00136
769.0
0.00662
0.00305
544300.0
4.69000
2.16000
16330.0
0.14100
0.06470
675.3
0.00581
0.00268
0.0
0.00000
0.00000
340.2
0.00293
0.00135
261.3
0.00225
0.00104
743.0
0.00640
0.00294
1043.0
0.00898
0.00413
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
860.0
0.00096
0.00088
1923.0
0.00216
0.00198
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
MASS OF EMISSIONS (1000 KG/YRI
PERCENT Of TOTAL INCLUDING METALLURGICAL PROCESSING
U)
SOURCE
GLYCERIN - CPtCHLOROHYORIN
GRAIN HARVESTING
GTPSUM
H V TRANSMISSION LINES
HANDLING OF CONCRETE PRODUCTS
HANDLING OF GRAIN
HEPTACHLOR
HEPTENE
HEXACHLOROBENZENE
HEXAMETHVLENETETRAMINE
HEXAHETHYLENEDIAHINE - ADIPONITRILE
HOSPITAL WASTE INCINERATION
HYDRAZINE
PART
S02
NOX
HC
CO
0.0
0.00000
0.00000
105500.0
0.08420
0.58800
99410.0
0.07930
0.55400
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
103.2
0.00089
0.0~0041
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
28540.0
0.02280
0.15900
25050.0
0.02000
0. 14000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
358.4
0.00029
0.00200
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
59.7
0.00026
0.00020
0.0
o.ooooo
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
59.7
0.00056
0.00027
1.4
0.00001
0.00001
136.1
0.00117
0.00054
5.4
0.00005
0.00002
276.3
0.00238
0.00109
13.9
0.00012
0.00006
358.4
0.00308
0.00142
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0,00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
448.0
0.00050
0.00046
-------
HASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
U>
SOURCE
HYDROCHLORIC ACID
HYOROQUINONE
HYOROXYLA«NE
HYDROXYLAHINE SULFATE
HYDROFLUORIC ACID
HYDROGEN CYANIDE
INCINERATION OF "TYPE 4" HASTE
INCINERATION OF "TYPE 0" HASTE
INCINERATION OF "TYPE 1" HASTE
INCINERATION OF "TYPE 2" HASTE
INCINERATION OF "TYPE 3" HASTE
INCINERATION OF "TYPE 5" HASTE
INCINERATION OF "TYPE 6" HASTE
PART
S02
NOX
HC
CO
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
2350.0
0.00167
0.01310
0.0
0.00000
0.00000
221.8
0.00016
0.00124
12040.0
0.00961
0.06710
S01SO.O
0.04000
0.27900
27620.0
0.02200
0.15400
7757.0
0.00619
0.04320
1416.0
0.00113
0.00789
36060.0
0.02880
0.20100
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
2007.0
0.00673
0.00666
6358.0
0.03640
0.02770
2302.0
0.01000
0.00764
646.4
0.00281
0.00215
0.0
0.00000
0.00000
6010.0
0.02620
0.02000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
365.4
0.00345
0.00163
433.2
0.00409
0.00194
1606.0
0.01520
0.00718
6686.0
0.06310
0.02990
2762.0
0.02610
0.01240
775.7
0.00733
0.00347
5244.0
0.04950
0.02350
4608.0
0.04540
0.02150
12.0
0.00010
0.00005
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
2.1
0.00002
0.00001
12040.0
0.10400
0.04770
50150.0
0.43200
0.19900
1381.0
0.01190
0.00547
387.8
0.00334
0.00154
196.6
0.00169
0.00076
36060.0
0.31000
0.14300
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0,00000
0.00000
71.0
0.00008
0.00007
16060.0
0.01800
0.01650
66860.0
0.07500
0.06870
32230.0
0.03610
0.03310
9049.0
0.01010
0.00930
13.1
0.00001
0.00001
48080.0
0.05390
0.04940
2
2
2
3
3
1
1
1
1
1
1
1
-------
SOURCE
INDUSTRIAL EXT COF1B BITUMINOUS PULV DRY BOTH
INDUSTRIAL EXT COMB BITUMINOUS PULV WET BOTH
INDUSTRIAL EXT COMB BITUMINOUS CYCLONE
INDUSTRIAL EXT CONB BITUMINOUS STOKER
INDUSTRIAL EXT COMB ANTHRACITE STOKER
CO
INDUSTRIAL EXT COMB LIGNITE STOKER
INDUSTRIAL EXT COMB RESID OIL TANG FIRE
INDUSTRIAL EXT COMB RESID OIL OTHER
INDUSTRIAL EXT COMB DIST OIL TANG FIRE
INDUSTRIAL EXT COMB DIST OIL OTHER
INDUSTRIAL EXT COMB GAS TANG FIRE
INDUSTRIAL ExT COMB GAS OTHER
INDUSTRIAL EXT COMB REFUSE
MASS OF EMISSIONS (1000 K6/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
66060.0
0.05270
0.36600
89670.0
0.07170
0.50100
5433.0
0.00433
0.03030
815900.0
0.65100
4.54000
5713.0
0.00456
0.03180
31590.0
0.02520
0.17600
7731.0
0.00617
0.04310
41670.0
0.03340
0.23300
2721.0
0.00217
0.01520
16330.0
0.01300
0.09100
2268.0
0.00181
0.01260
19960.0
0.01590
0.11100
228900.0
0.18300
1.28000
406100.0
1.78000
1.35000
199700.0
0.86900
0.66300
61570.0
0.26600
0.20400
776000.0
3.36000
2.58000
6621.0
0.02880
0.02200
22490.0
0.09790
0.07470
145400.0
0.63300
0.48300
763400.0
3.32000
2.53000
5442.0
0.02370
0.01810
31720.0
0.13800
0.10500
127.1
0.00055
0.00042
1179.0
0.00513
0.00392
16390.0
0.07130
0.05440
223800.0
2.11000
1.00000
79070.0
0.74700
0.35400
44370.0
0.41900
0.19600
150800.0
1.42000
0.67400
1717.0
0.01620
0.00766
16360.0
0.15500
0.07330
37180.0
0.35100
0.16600
197800.0
1.67000
0.88500
9070.0
0.08570
0.04060
90740.0
0.85700
0.40600
38070.0
0.36000
0.17000
344600.0
3.25000
1.54000
131900.0
1.25000
0.59000
682.5
0.00587
0.00270
790.7
0.00681
0.00313
244.4
0.00210
0.00097
9977.0
0.06590
0.03950
49.9
0.00043
0.00020
1270.0
0.01090
0.00503
638.1
0.00549
0.00253
2722.0
0.02340
0.01080
596.6
0.00515
0.00237
3172.0
0.02730
0.01260
699.5
0.00602
0.00277
6256.0
0.05390
0.02480
33050.0
0.28400
0.13100
0.0
0.00000
0.00000
2631.0
0.00295
0.00270
606.5
0.00090
0.00083
2016.0
0.00226
0.00207
1542.0
0.00173
0.00158
12700.0
0.01420
0.01300
3448.0
0.00367
0.00354
13390.0
0.01520
0.01400
807.2
0.00090
0.00083
4350.0
0.00486
0.00447
3715.0
0.00417
0.00382
33640.0
0.03770
0.03460
35900.0
0.04020
0.03690
-------
SOURCE
MASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
INDUSTRIAL INT COMB DIST OIL TURBINE
INDUSTRIAL INT COMB GAS TURBINE
INDUSTRIAL INT COMB DIST OIL RECIP ENG
INDUSTRIAL INT COMB GAS RECIP ENG
INDUSTRIAL SAND HANDLING
w IRON FOUNDRIES
~J
IRON CHLORIDE • FERRIC
IRON OXIDE - PIGMENTS
ISOCYANATES
ISOOCTAL ALCOHOLS
ISOPHTHALIC ACID
ISOPROPYL ACETATE
ISOPRENE - 2-METHYL-1.3-BUTAOIENE
1542.0
0.00123
0.00859
0.0
0.00000
0.00000
3359.0
0.00268
0.01870
0.0
0.00000
0.00000
3560.0
0.00284
0.01470
153600.0
0.12300
0.85500
34.9
0.00003
0.00019
2901.0
0.01260
0.00963
226.7
0.00099
0.00075
3263.0
0.01420
0.01060
154.4
0.00067
0.00051
0.0
0.00000
0.00000
0.0
0.00000
0.00000
10880.0
0.10300
0.04870
226700.0
2.14000
1.01000
47150.0
0.44500
0.21100
749400.0
7.04000
3.33000
8875.0
0.08380
0.03970
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
3806.0
0.03280
0.01510
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
o.ooooo
0.00000
0.0
0.00000
0.00000
9973.0
0.01120
0.01020
0.0
0.00000
0.00000
1287000.0
1.44000
1.32000
0.0
0.00000
0.00000
1
1
1
1
4
3
3
360. S
0.00029
0.00201
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
9.1
0.0000"*
0.00003
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
984.1
0.00503
0.00231
43.1
0.00037
0.00017
104.3
0.00090
0.00041
18.1
0.00016
0.00007
177.3
0.00153
0.00070
38810.0
0.04350
0.03990
64.6
0.00007
0.00007
547.7
0.00061
0.00056
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
SOURCE
MASS OF EMISSIONS (1000 KG/YRI
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
LO
CO
ISOPROPANOL - DIRECT HYORATION
JET ENGINE TESTING
KETONE ALCOHOL OIL
LAND CLEARING • OPEN BURNING
LEAD CARBONATE AND SULFATE - WHITE LEAD
LEAD OXIDE - RED LEAD AND LITHARGE - PIGMENTS ONLY
LEAD CHROHATE - CHROME YELLOW AND ORANGE
LEAD COMPOUNDS • HALIOES, HYDROXIDESt DIOXIDE. NITRATE* ETC.
LEAD ARSENATE
LEATHER
LIME KILNS
LINDANE
LINEAR ALKYLBENZENE
0.0
0.00000
0.00000
26ft,9
0.00021
0.00150
0.0
0.00000
0,00000
140.0
0.00035
0. 0021*3
312400.0
0.24900
1.74000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
112.6
0.00049
0.00037
0.0
0.00000
0.00000
440.0
0.00191
0.00146
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
330.S
0.00312
0.00118
0.0
0.00000
0.00000
110.0
0.00104
0.00049
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
9.3
o.ooooe
0.00004
472,5
0,00407
0.00187
389.9
0.00336
0.00154
1100.0
0.00947
0.00436
0.0
0.00000
0.00000
0.5
0.00000
0.00000
13.7
0.00012
0.00005
0.0
0.00000
0.00000
1220.0
0.00137
0.00125
431.7
0.00048
0.00044
2.3
0.00000
0.00001
37.1
0.00003
0.00021
1.5
0.00000
0.00001
0.5
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
»4.0
0.00005
0.00005
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
SOURCE
MASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING HETALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
U>
VD
LINEAR ALCOHOLS • ZIEGLER PROCESS
LINURON
LITHIUM SALTS - LITHIUM CARBONATE AND LITHIUM HYDROXIDE
LOADING OF SAND AND GRAVEL
LOADING HYDRAULIC CEMENT
LOADING READY-MIX CEMENT
LOADING OF FINISHED CLAY
LOADING LIME
MAGNESIUM COMPOUNDS - CARBONATE. CHLORIDE* OXIDE t HYDROXIDE
MALATHION
MALEIC ANHYDRIDE FROM BENZENE
HALT BEVERAGE PRODUCTION
MANEB
0.0
0.00000
0.00000
0.0
0.00000
0.00000
3.2
0.00000
0.00002
20S60.0
0.01660
0.06020
3117.0
0. 00219
0.01120
53m. 0
0. 00426
0.02010
256.6
0.00021
0.00069
356.3
0.00028
0.00117
3033.0
0.00242
0.01690
6.6
0.00001
0.00004
19.2
0.00002
0.00011
106500.0
0.06660
0.60400
2.7
0.00000
0.00002
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
4.4
0.00002
0.00001
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1116.0
0.00466
0.00370
0.0
0.00000
0.00000 •
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
3.7
0.00003
0.00002
57.6
0.00054
0.00026
0.0
0.00000
0.00000
0.0
0.00000
0.00000
59.0
0.00051
0.00023
0.7
0.00001
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
27.2
0.00023
0.00011
156600.0
1.35000
0.62100
67610.0
0.56400
0.26900
6.2
0.00007
0.00003
0.0
0.00000
0.00000
0.0
0.00000
0,00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
121600.0
0.13600
0.12500
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
SOURCE
MASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
MANGANESE SULFATE .
MANUFACTURE OF ASBESTOS PRODUCTS - WEAVING
MANUFACTURE OF COTTON FABRICS
MANUFACTURE OF LINEN CLOTH
MANUFACTURE AND PROCESSING OF ROPE
MANUFACTURE OF WOOL CLOTH
MEAT SMOKEHOUSES
MELAMINE
MERCURY COMPOUNDS - HALIOES, NITRATES, OXIDES* ETC*
MERPHOS
METALKAMATE (BUX)
METHANOL
METHANEARSONIC ACID - DODECYL AND OCTYL AMMONIUM SALTS
34.e
0.00009
0.00019
15.7
0.00001
0.00008
1075.0
0.00086
0.00599
1.8
0.00000
0.00001
<»6.7
0.00004
0.00026
22.1
0.00002
0.00012
68.1
0.00005
0.00038
92.0
0.00004
0.00029
0.5
0.00000
0.00000
0.0
0,00000
0.00000
2.3
0.00000
0.00001
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
if 64. 9
0.00202
0.00154
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0,00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0,00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
102.1
0.00088
0.00040
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
6.8
0.00006
0.00003
17090.0
0.14700
0.06770
2. a
0.00002
0,00001
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
o.ooooo
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
17090.0
0.01920
0.01760
0.0
0.00000
0.00000
-------
MASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
SOURCE
METHANE ARSENIC ACID
2-METHOXYETHANOL
NETHOXYCHLOR
METHYLENE CHLORIDE - CHLORINATION OF METHANE
METHYLENE DIPHENYLOIISOCYANATE
METHYL HETHACRTLATE
METHYL ISOBUTTL KCTONE
HETHYL ACETATE
HETHYL ETHYL KETONE
HETHYL PARATHION
HETHYL BROHIOE
METHYL CHLORIDE
METHYL MERCAPTAN
PART
0.0
0.00000
0.00000
2.3
0.00000
0.00001
0.0
0.00000
0.00000
S02
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
NOX
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
HC
43.8
0.00036
0.00017
2.3
0.00002
0.00001
4241.0
0.03650
0.01660
CO
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0,00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
23.6
0.00002
0.00013
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
9671.0
0.04210
0.03210
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
23440.0
0.20200
0.09290
S24B.O
0.04920
0.02060
4.1
0.00004
0.00002
159.9
0.00136
0.00063
23.6
0.00020
0.00009
7.0
0.00006
0.00003
3617.0
0.03290
0.01510
4.5
0.00004
0.00002
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
SOURCE
MASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
MEVINPHOS
MINERAL WOOL
MINING AND BLASTING OF ASBESTOS ORE
MISCELLANEOUS SODIUM COMPOUNDS
MIXED LINEAR ALCOHOL
MIXED OLEFINIC PRODUCT
MIXED CRESOLS
HOOACRYLIC FIBERS
HONOCROTOPHOS
MONOETHYLAMINE
MONOSODIUH 6LUTAHATE
MONURON
MSMA
0.2
0.00000
0.00000
166700.0
0.13300
0.92900
419.6
0.00033
0.00212
56.7
0.00005
0.00032
0.0
0.00000
0.00000
0.0
0.00000
0.00000
16920.0
0.07360
0.05620
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
8061.0
0.07610
0.03610
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.2
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
4ei,4
0.00414
0.00191
0.0
0.00000
0.00000
3735.0
0.00419
0.00384
0.0
0.00000
0.00000
240.7
0.00027
0.00029
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1.6
0.00000
0.00001
0.0
0.00000
0.00000
0.0
0.00000
O.'OOOOO
0.0
0.00000
0.00000
o.o
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
65.1
0.00061
0.00029
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
31.0
0.00027
0.00012
317.3
0.00273
0.00126
1.6
0.00001
0.00001
6.4
0.00005
0.00003
9.6
o.ooooa
0.00004
0.2
0.00000
0.00000
17.4
0.00015
0.00007
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
O.OOOOD
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
SOURCE
MASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
U)
MUNICIPAL DUMPS - OPEN BURNING
MUNICIPAL INCINERATION
NABAM
NALEO
NAPHTHALENE - COAL TAR
NAPHTHALENE
NAPHTHENIC ACID • COPPER SALT
NATURAL FIRES
NATURAL GAS DISTRIBUTION
NATURAL GAS EXTRACTION
NATURAL GAS PROCESSING
NICKEL COMPOUNDS - EXCEPT NICKEL SULFATE
NICKEL SULFATE
227300.0
0.18100
1.27000
1.1
0.00000
0.00001
0.5
0.00000
0.00000
0.0
0.00000
0.00,000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
18940.0
0.08240
0.06290
464.9
0.00202
0.00154
0.0
0.00000
0.00000
200.9
0.00087
0.00067
0.0
0.00000
0.00000
0.0
0.00000
0.00000
22730.0
0.21500
0.10200
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
733.5
0.00693
0.00328
0.0
0.00000
0.00000
11360.0
0.09780
0.04500
3.4
0.00003
0.00001
0.5
0.00000
0.00000
1205.0
0.01040
0.00477
349.3
0.00301
0.00138
1.5
0.00001
0.00001
265100.0
0.29700
0.27200
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
2.7
0.00000
0.00002
9.9
0.00001
0.00006
0.0
0.00000
0.00000
0.0
0.00000
0.00000
571500.0
2.49000
1.90000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
905000.0
7.79000
3.59000
54370.0
0.46900
0.21500
762000.0
6.56000
3.02000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
SOURCE
MASS OF EMISSIONS 11000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
NITRIC ACID
NITROBENZENE
P-NITROPHENOL
NITROGLYCERINE
NITROCELLULOSE
NITROCHLOROBENZENE
NITROPARAFINS
NITROANILINE
NONENE - NON-LINEAR
NONYLPHENOL
NYLON 66
NYLON 6
N-OCTYL-N-DECYL PHTHALATE
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
19050.0
0.01320
0.10600
9089.0
0.00725
0.05060
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
29.5
0.00013
0.00010
0.0
0.00000
0.00000
0.0
0.00000
0.00000
2.9
0.00001
0.00001
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
27090.0
0.25500
0.12100
102.2
0.00096
0.00046
22.5
0.00021
0.00010
0.9
0.00001
0.00000
18.6
0.00018
0.00008
27.8
0.00026
0.00012
7.1
0.00007
0.00003
2.9
0.00003
0.00001
0.0
0.00000
0.00000
0.0
0.00000
0.00000
31.8
0.00030
0.00014
15.1
o.ooom
0.00007
0.0
0.00000
0.00000
0.0
0.00000
0.00000
3392.0
0.02920
0.01340
33.8
0.00029
0.00013
0.0
0.00000
0.00000
0.0
0.00000
0.00000
99.0
0.00085
0.00039
0.0
0.00000
0.00000
2.9
0.00002
0.00001
707.6
0.00609
0.00280
80.6
0.00069
0.00032
2858.0
0.02460
0.01130
1363.0
0.01170
0.00540
26.7
0.00023
0.00011
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0,00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
MASS OF EMISSIONS (1000 KG/YRI
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
ui
SOURCE
OCTYLPHENOL
OLEIC ACID
ON SITE BURNING - OPEN BURNING
OPEN BURNING OF AUTO BODIES
OPEN PIT INCINERATION
OPEN BURNING OF INDUSTRIAL WASTE
OPEN BURNING OF JET FUEL
OPEN BURNING OF WOOD WASTE
OPEN BURNING OF RAIL CARS
OPEN STORAGE OF SAND AND GRAVEL
OPEN MINING AND STORAGE OF MICA
OPEN MINING AND GRINDING OF PUMICE
OPEN CLAY MINING
PART
S02
NOX
HC
CO
0.0
0,00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1.6
0.00001
0.00001
29.9
0.00026
0.00012
0.0
0.00000
0.00000
0.0
0.00000
0.00000
911.7
0.00073
0.00508
13140.0
0.01050
0.07320
288.9
0.00023
0.00161
3950.0
0.00315
0.02200
1644.0
0.00131
0.00916
45880.0
0.03660
0.17600
59.4
0.00005
0.00021
451.2
0.00036
0.00191
25.9
0.00002
0.00009
44.2
0.00019
0.00015
821.0
0.00357
0.00273
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
159.9
0.00151
0.00071
4926.0
0.04650
0.02200
74.3
0.00070
0.00033
464.7
0.00439
0.00208
193.5
0.00183
0.00086
0.0
0.00000
0.00000
24630.0
0.21200
0.09760
288.9
0.00249
0.00114
929.4
0.00800
0.00368
386.9
0.00333
0.00153
0.0
0.00000
0.00000
69790.0
0.07820
0.07170
825.6
0.00093
0.00085
11620.0
0.01300
0.01190
4837.0
0.00542
0.00497
-------
MASS OF EMISSIONS (1000 KG/TR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
cn
SOURCE
OPEN MINING OF COAL
OPEN MINING OF TALC
ORCHARD HEATING
OXALIC ACID
0X0 MIXED LINEAR ALCOHOLS
0X0 PROCESS
PAINT MANUFACTURING
PAPER MILL BUILDING EMISSIONS
N-PARAFFINS
N-PARAFFIN CHLORIDE
PARAFORMALDEHYDE
PARATHION
PARATHION APPLICATION ON CROPS
PART
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
7.7
0.00001
0.00001*
S02
NOX
HC
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
3162.0
o.oiseo
0.01050
800.2
0.00756
0.00398
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
381.0
0.00328
0.00151
66.5
0.00097
0.00026
4.9
0.00004
0.00002
7.8
0.00007
0.00003
CO
3426.0
0.00273
0.01910
566.1
0.00045
0.00226
79290.0
0.06000
0.41900
17.1
0.00001
0.00010
3.9
0.00000
0.00002
3.8
0.00000
0.00002
476.2
0.00038
0.00265
220900.0
0.95900
0.73200
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
42.9
0.00040
0.00019
31.3
0.00030
0.00014
30.5
0.00029
0.00014
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
2374.0
0.02040
0.00940
2308.0
0.01990
0.00915
7143.0
0.06130
0.02830
4242000.0
4.76000
4.36000
0.0
0.00000
0.00000
8813.0
0.00988
0.00905
8571.0
0.00961
0.00880
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
SOURCE
MASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
PENICILLIN 6 - PROCAINE
PENICILLIN 6 - POTASSIUM
PENTAERYTHRITOL
PENTAERYTHRIOL TETRANITRATE
PENTACHLOROPHENOL AND SODIUM SALTS
PERCHLOROETHYLENE - FROM TRICHLOROETHYLENE
PERCHLOROETHYLENE - CHLORINATION OF PROPANE
PERLITE MANUFACTURING
PETROLEUM EXTRACTION
PETROLEUM REFINING • ALKYLATION
PETROLEUM REFINING - AROMATICS/ISOHERIZATION
PETROLEUM REFINING - ASPHALT PLANT
PETROLEUM REFINING - BLENDING AND STORAGE
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0,00000
0.00000
0.0
0.00000
0.00000
64.9
0.00005
0.00036
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
9.3
0.00009
0.00004
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.2
0.00000
0.00000
1.0
0.00001
0.00000
979.6
0.00643
0.00386
9.6
0.00005
0.00002
23.6
0.00020
0.00009
271.9
0.00234
0.00106
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1935.0
0.00154
0.01060
0.0
0.00000
0.00000
1.4
0.00000
0.00001
6.3
0.00000
0.00003
5652.0
0.00467
0.03260
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
11.6
0.00005
0.00004
17.9
0.00006
0.00006
4755.0
0.02070
0.01560
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
2.3
0.00002
0.00001
6.9
0.00008
0.00004
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
111500.0
0.95900
0.44200
0.3
0.00000
0.00000
0.6
0.00001
0.00000
7498.0
0.06450
0.02970
215600.0
1.86000
0.65400
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.2
0.00000
0.00000
0.9
0.00000
0.00000
31090.0
0.03490
0.03190
0.0
0.00000
0.00000
-------
CO
SOURCE
PETROLEUM REFINING • CATALYTIC CRACKING
PETROLEUM REFINING • CATALYTIC HYOROREFINING (HDS)
PETROLEUM REFINING » CATALYTIC REFORMING
PETROLEUM REFINING • CRUDE DISTILLATION
PETROLEUM REFINING - FLARES
PETROLEUM REFINING - FUGITIVE EMISSIONS
PETROLEUM REFINING - SULFUR PLANT
PETROLEUM REFINING • VACUUM DISTILLATION
PETROLEUM REFINING - WASTE HATER PLANT
PHENYLMERCURY OLEATE
PHENYLMERCURY ACETATE - PHA - PMAS
PHORATE
PHOSGENE
MASS OF EMISSIONS (1000 KS/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
4i48o.o
0.03310
0.23100
1202.0
0.00096
0.00669
1667.0
0.00133
0.00929
3 1*820.0
0.02780
0.191*00
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
2.3
0.00000
0.00001
0.0
0.00000
0.00000
488800.0
2.13000
1.62000
2518.0
0.01100
0.00836
3427.0
0.01190
0.01140
278600.0
1.21000
0.92500
62180.0
0.27100
0.20600
0.0
0.00000
0.00000
28810.0
0.12500
0.09560
0.0
0.00000
0.00000
0.0
0.00000
o.oooob
0.0
0.00000
0.00000
0.0
0.00000
0.00000
929.9
0.00405
0.00309
0.0
0.00000
0.00000
60730.0
0.57l»00
0.27200
211*6.0
0.02030
0.00960
2872.0
0.02710
0.01280
69640.0
0.65800
0.31200
7876.0
0.07440
0.03520
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
208900.0
1.80000
0.82800
85.8
0.00074
0.00034
185.3
0.00159
0.00073
6840.0
0.05890
0.02710
1534.0
0.01320
0.00608
912000.0
7.85000
3.61000
0.0
0.00000
0.00000
92470.0
0.79600
0.36600
257000.0
2.21000
1.02000
1815.0
0.01560
0.00719
0.1
0.00000
0.00000
0.0
0.00000
0.00000
0.4
0.00000
0.00000
1185.0
0.00133
0.00122
200.3
0.00022
0.00021
277.9
0.00031
0.00028
6964.0
0.00781
0.00715
2985.0
0.00335
0.00307
0.0
0.00000
0.00000
28810.0
0.03230
0.02960
3884.0
0.00433
0.00399
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.4
0.00000
0.00000
-------
MASS OF EMISSIONS (1000 K6/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
vo
SOURCE
PHOSPHORIC ACID - WET PROCESS
PHOSPHORIC ACIO - THERMAL PROCESS
PHOSPHATE ROCK - DRYING. GRINDING. CALCINING
PHOSPHARIDION
PHOSPHATE ROCK DEFLUORINATION
PHOSPHORUS - ELEMENTAL
PHOSPHORUS OXYCHLORIDE
PHOSPHORUS TRICHLORIDE
PHOSPHORUS PENTASULFIOE
PHOSPHATE ROCK OPEN STORAGE
PHOSPHATE ROCK LOADING
PHTHALIC ANHYDRIDE - 0-XYLENE
PHTHALIC ANHYDRIDE - NAPHTHALENE
PIG IRON PRODUCTION
PART
3S510.0
0.02830
0.17100
22600.0
0.01800
0.10900
123.5
0.00010
0.00069
62.1
0.00005
0.00035
1281000.0
1.02000
7.13000
S02
1647.0
0.00717
0.00547
0.0
0.00000
0.00000
55000.0
0.23900
0.18300
NOX
HC
452.8
0.00428
0.00203
227.7
0.00215
0.00102
40140.0
0.37900
0.18000
65050.0
0.56000
0.25800
83750.0
0.72100
0.33200
0.0
0.00000
0.00000
CO
1734.0
0.00138
0.00966
1328.0
0.00122
0.00851
20970.0
0.01640
0.11500
0.2
0.00000
0.00000
—
"
--
«
..
222.0
0.00097
0.00074
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
—
"
—
"
..
0.0
0.00000
0.00000
41.7
0.00039
0.00019
0.0
0.00000
0.00000
0.0
0.00000
0.00000
"
—
"
"
„
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.2
0.00000
0.00000
..
—
"
«
..
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0,0
0.00000
0.00000
0.0
0.00000
0.00000
—
«
—
—
.
3
3
3
2
3
3
3
3
3
452.8
0.00051
0.00046
215.2
0.00024
0.00022
71050000.0
79.70000
73.00000
-------
SOURCE
PLASTICS PROCESSING
PLYWOOD AND VENEER DRYING
POLYAMIOE RESINS
POLYACRYLONITRILE — POLYMERIZATION SOLUTION
POLYBUTADIENC
tn
O
POLYCHLOROPRENE
POLYCARBONATE RESINS
POLYCHLORINATEO BIPHENYLS
POLYESTER RESINS - UNSATURATED
POLYETHYLENE RESIN - LOU DENSITY
POLYETHYLENE RESIN - HIGH DENSITY
POLYESTER POLTOLS
POLYISOPRENE
"ASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
194300.0
0.12300
0.66000
0.0
0.00000
0.00000
5.7
0.00000
0.00003
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
o.o
0.00000
0.00000
o.o
0.00000
0.00000
0.0
0.00000
0.00000
599.1
0.00046
0.00334
0.0
0.00000
0.00000
0.0
0.00000
0.00000
o.o
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.2
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
462900.0
3.98000
1.83000
9169.0
0.07890
0.03630
857.6
0.00738
0.00340
113.4
0.00098
0.00043
1173.0
0.01010
0.00465
1371.0
0.01180
0.00543
4.0
0.00003
0.00002
110.0
0.00095
0.00044
1115.0
0.00960
0.00442
23960.0
0.20600
0.09490
28220.0
0.24300
0.11200
81.0
0.00070
0.00032
112.3
0.00097
0.00044
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
MASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
SOURCE
POLYHETHYLENE POLYPHENYL ISOCYANATE
POLYPROPYLENE
POLYSTYRENE RESIN
POLYSULFIDE RUBBER
POLYURETHANE SURFACE COATING RESINS
01 POLYURETHANE ELASTOMER
POLYURETHANE FIBERS
POLYVINYL ACETATE RESINS
POLYVINYL CHLORIDE
POLYVINYL ALCOHOL RESINS
POLYVINYLVINYLIDENE CHLORIDE
POTASSIUM HYDROXIDE
POTASSIUM SULFATE
PART
366.5
0.00029
0.00204
S02
0.0
0.00000
0.00000
NOX
0.0
0.00000
0.00000
HC
0.0
0.00000
0.00000
CO
0.0
0.00000
0.00000
0.0
0.00000
0.00000
293.4
0.00023
0.00163
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
16610.0
0.01330
0.09250
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
966.3
0.00421
0.00321
21.8
0.00009
0.00007
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.5
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
208.7
0.00180
0.00083
9768.0
0.08410
0.03870
17110.0
0.14700
0.06780
21.8
0.00019
0.00009
22.5
0.00019
0.00009
22.5
0.00019
0.00009
4.1
0.00004
0.00002
301.9
0.00260
0.00120
78650.0
0.67700
0.31200
184.9
0.00159
0.00073
123.8
0.00107
0.00049
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
ui
NJ
SOURCE
POTASH - POTASSIUM SALTS
POTASSIUM PERMANGANATE AND MANGANESE DIOXIDE
POTASSIUM BICHROMATE AND POTASSIUM CHROMATE
POULTRY DRESSING
PREPARATION OF ASBESTOS FIBRES
PREPARATION OF COTTON FIBRES
PRESCRIBED BURNING
PRIMARY LEAD SMELTING AND REFINING
PRIMARY ALUMINUM PRODUCTION
PRIMARY ZINC SMELTING
PRIMARY COPPER SMELTING
PRINTING INK
PRINTING COTTON FABRICS
MASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
23610.0
0.01880
0.13100
17.6
0.00001
0.00010
0.2
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
37.8
0.00003
0.00021
20280.0
0.01620
0.11300
383800.0
0.30600
2.14000
3879.0
0.00309
0.02160
140600.0
0.11500
O.A0500
46790.0
0.03730
0.26000
6123.0
0.00489
0.03410
226.7
0.00018
0.00126
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
41970.0
0.18300
0.13900
0.0
0.00000
0.00000
5744.0
0.02500
0.01910
99790.0
0.43400
0.33100
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
99800.0
0.94300
0.44600
316.0
0.00300
0.00142
0.0
0.00000
0.00000
287.2
0.00271
0.00128
798.3
0.0075*
0.00357
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
99800.0
0.85900
0.39500
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
17000.0
0.14600
0.06740
74100.0
0.63800
0.29400
0.0
0.00000
0.00000
0.0
0.00000
0.00000
752300.0
0.84400
0.77300
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
SOURCE
MASS OF EMISSIONS (1000 KS/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
Ul
U>
PRINTING LINEN FABRICS
PRINTING NATURAL POLYMER FABRICS
PRINTING RATON FABRICS
PRINTING SILK FABRICS
PRINTING WOOL FABRICS
PRINTING SYNTHETIC POLYMER FABRICS
PRODUCTION OF LEAD-ACID BATTERIES
PROPACHLOR
PROPANIL
PROPAZINE
PROPIONIC ACID
PROPYLENE
PROPYLENE OXIDE - CHLOROHYDRIN PROCESS
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0,00000
0.00000
3106.0
0.00248
0.01730
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
12600.0
0.11900
0.05630
0.0
0.00000
0.00000
595.8
0.00513
0.00236
7779.0
0.06700
0.03080
31120.0
0.26800
0.12300
519.1
0.00447
0.00206
5133.0
0.04420
0.02030
9837.0
0.08470
0.03900
0.0
0.00000
0.00000
10.2
0.00009
0.00004
3.4
0.00003
0.00001
6.8
0.00006
0.00003
147.0
0.00126
0.00058
5998.0
0.05160
0.02380
13360.0
0.11500
0.05290
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
24.5
0.00003
0.00003
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
MASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
SOURCE
PROPYLENE GLYCOL
N-PROPYL ALCOHOL
PROPYLENE TETRAHER
PROPYLENE TRIHER
PYRETHINS
U1 PYR06ALLIC ACID
QUINOLINE
RAYON - SEMI SYNTHETIC VISCOSE RAYON
RECLAIMING OF HASTE SOLVENTS
REFRACTORIES
REFRIGERATION
REFUSE UNLOADING
REFUSE ASH DISPOSAL
PART
7287.0
0.00381
0.04060
459.0
0.00037
0.00256
SOS
NOX
HC
CO
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.5
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
37290.0
0.02970
0.20700
133700.0
0.10700
0.74500
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
376.6
0.00324
0.00149
94.2
o.oooai
0.00037
313.0
0,00269
0.00124
210.9
0,00162
0,00061
0.9
0,00000
0,00000
0.5
0.00000
0.00000
0.9
0.00001
0.00000
1217.0
0.01050
0.00462
106600.0
0.99500
0.43000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0,00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
2
2
2
2
2
2
2
2
2.
3
-------
SOURCE
MASS OF EMISSIONS (1000 K6/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
cn
cn
RESIDENTIAL INCINERATION
RESIDENTIAL EXT COMB BITUMINOUS
RESIDENTIAL EXT COMB ANTHRACITE
RESIDENTIAL EXT COMB LIGNITE
RESIDENTIAL EXT COMB DIST OIL
RESIDENTIAL EXT COMB GAS
RESIDENTIAL EXT COMB WOOD
RESORCINOL
ROCKET ENGINE TESTING
RONNEL
RUBBER PROCESSING
SACCHARIN - VIA 0-TOLUENE SULFONAHIDE
SACCHARIN
153800.0
0.12300
0.85700
8985.0
0.00717
0.05000
937.2
0.00075
0.00522
18.0
0.00001
0.00010
7 1*330.0
0.05930
0.41400
47340.0
0.03780
0.26400
61400.0
0.04900
0.34200
0.0
0.00000
0.00000
2563.0
0.01120
0.00851
66520.0
0.28900
0.22100
6901.0
0.03000
0.02290
121.7
0.00053
0.00040
1089000.0
4.74000
3.62000
1361.0
0.00592
0.00452
1445.0
0.00629
0.00480
0.0
0.00000
0.00000
15380.0
0.14500
0.06880
6220.0
0.05880
0.02780
766.8
0.00724
0.00343
59.9
0.00057
0.00027
89050.0
0.84100
0.39800
190400.0
1.80000
0.85200
16610.0
0.15700
0.07430
0.0
0.00000
0.00000
76890.0
0.66200
0.30500
6739.0
0.05800
0.02670
1108.0
0.00933
0.00439
10.0
0.00009
0.00004
22670.0
0.19500
0.08980
19040.0
0.16400
0.07540
63010.0
0.56000
0.25800
17.1
0.00015
0.00007
102500.0
0.11500
0.10500
29370.0
0.03290
0.03020
7072.0
0.00793
0.00726
20.0
0.00002
0.00002
37170.0
0.04170
0.03820
49070.0
0.05500
0.05040
411700.0
0. 46200
0.42300
0.0
0.00000
0.00000
. 0.5
0.00000
0.00000
12790.0
0.01020
0.07130
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.3
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.2
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
o.e
0.00001
0.00000
1.8
0.00002
0.00001
38540.0
0.50400
0.23200
0.7
0.00001
0.00000
0.4
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
o.ooooo
0.00000
0.0
0.00000
0.00000
-------
MASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
Ul
CTl
SOURCE
SALICYLIC ACIO
SALICYLATES - EXCLUDING ASPIRIN
SAND AND GRAVEL UNLOADING
SAW HILL WASTE STORAGE
SCOURING WOOL FIBRES
SCREENING* CRUSHING OF CLAY
SECONDARY LEAD SMELTING AND REFINING
SECONDARY ALUMINUM PRODUCTION
SECONDARY ZINC SMELTING
SECONDARY MAGNESIUM SMELTING
SEWAGE SLUDGE INCINERATION
SEWERAGE CHLQRINATION TANKS
SEWERAGE AERATION
SEWERAGE TRICKLING FILTER
PART
S02
NOX
HC
CO
0.0 0.0
0.00000 0.00000
0.00000 0.00000
16690.0
0.01330
0.06420
1634.0
0.00130
0.00652
0.0 0.6 0.0
0.00000 0.00001 0.00000
0.00000 0,00000 0.00000
51720.0
0.04130
0.17700
3853. 0
0.00307
0.02150
43950.0
0.03510
0.24500
3518.0
0.00281
0.01960
2.8
0.00000
0.00002
13610.0
0.01090
0.07580
16870.0
0.07340
0.05600
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1134.0
0.00493
0.00376
261.2
0.00266
0.00126
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1361.0
0.01290
0.00609
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0,00000
0.00000
0.0
0.00000
0.00000
680.4
0.00586
0.00270
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0,00000
0.00000
0.0
0.00000
0.00000
15880.0
0.01780
0.01630
-------
Ul
SOURCE
SEWERAGE VACCUUH FILTER
siLvex
SILVER COMPOUNDS - N03< DIFLUORIDE. FLUOROBORATEt S04
SIMAZINE
SINGEING COTTON FABRICS
SINGEING LINEN FABRICS
SIZING. GRINDING. FIBERIZING OF ASBESTOS
SOAP AND DETERGENTS
SODIUM ARSENlTE
SODIUM SILICATES
SODIUM TCA
SOOIUH CARBONATE - SYNTHETIC
sooiun NITRITE
MASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
0.7
0.00000
0.00000
i.a
0.00000
0.00001
0.0
0.00000
0.00000
62.6
o.oooos
0.00035
0.1
0.00000
0.00000
840.5
0.00067
0.00168
18370.0
0.01470
0.10200
2.6
0.00000
0.00001
960.7
0.00077
0.00535
0.0
0.00000
0.00000
1414.0
0.00113
0.00788
7.6
0.00001
0.00004
0.0
0.00000.
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
31.4
0.00014
0.00010
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1310.0
0.00570
0.00435
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
ie.o
0.00017
0.00008
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
3493.0
0.03300
0.01560
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1.4
0.00001
0.00001
0.0
0.00000
0.00000
10.2
0.00009
0.00004
26.9
0.00023
0.00011
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
87.3
0.00075
0.00035
6.8
0.00006
0.00003
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
9.0
0.00001
0.00001
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
436.7
0.00049
0.00049
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
Ul
00
SOURCE
SODIUM SULFITE
SODIUM HYDROSULFITE
SODIUM CARBONATE - NATURAL
SODIUM SULFATE - NATURAL PROCESS ONLY
SODIUM CHROMATE AND SODIUM OICHROMATE
SODIUM HYOROSULFIDE - SODIUM BISULFIDE OR SULFHYDRATE
SODIUM CHLORATE
SODIUM SULFloE
SODIUM THIOSULFATC • SODIUM HYPOSULFITE
SODIUM TRIPOLYPHOSPHATE
SODIUM SILICOFLUORIDE
SODIUM FLUORIDE
SOLVENT EVAPORATION - ORYCLEANIN6
MASS OF EMISSIONS (1000 K6/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
201.4
0.00016
0.00112
12.3
0.00003
0.00023
8299.0
0.00662
0.04620
2310.0
0.00184
0.01290
146.7
0.00012
0.00082
201.4
0.00088
0.00067
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
66.7
0.00029
0.00022
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
66.7
0.00063
0.00030
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
66.7
0.00007
0.00007
176.0
0.00014
0.00098
783.8
0.00062
0.00437
39.2
0.00003
0,00022
5699.0
0.00455
0.03170
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
O.QOOOO
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
2166000.0
18.60000
8.58000
0.0
0.00000
0.00000
-------
Ul
vo
SOURCE
SOLVENT EVAPORATION - PRINTING AND PUBLISHING
SOLVENT EVAPORATION - DECREASING
SOLVENT EVAPORATION - SURFACE COATING - AUTO PAINTING
SORBITOL
SPINNING ASBESTOS FIBRES - TWISTING AND WINDING
SPINNING NATURAL POLYMER FIBRES
SPINNING RAYON FIBRE
SPINNING SYNTHETIC POLYHERS
STEEL PRODUCTION
STEEL FOUNDRIES
STORAGE OF ANIMAL RENDERINGS
STORAGE OF ASBESTOS ORE
STORAGE OF SAWDUST
MASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1387.0
0.00111
0.00773
0.0
0.00000
0.00000
65.2
0.00005
0.00036
34.9
0.00003
0.00019
139.4
0.00011
0.00078
2621.0
0.00209
0.01460
570400.0
0.45500
3.18000
11940.0
0.00953
0.06650
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
60490.0
0.57100
0.27100
183.7
0.00173
0.00082
182200.0
1.57000
0.72200
514300.0
4.43000
2.04000
73210.0
0.63000
0.29000
26.6
0.00023
0.00010
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
5154000.0
5.78000
5.29000
0.0
0.00000
0.00000
2
2
2
2
2
2
2
2
3
3
178.1
0.00014
0.00091
1433.0
0.00114
0.00540
-------
MASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
SOURCE
STORAGE OF WOOD CHIPS
STORAGE OF R«W CLAY
STORAGE OF TALC ORE
STORAGE OF SULFUR
STRUCTURAL FIRES
STYRCNE - BUTADIENE COPOLYMER RESINS
STYRENE
SUGAR PROCESSING
SULFATED ETHoXYLATES - AEOS
SULFURIC ACID
SULFUR HONOCHLORIOE AND DICHLORIOE
SUPERPHOSPHATE - NORMAL
SUPERPHOSPHORIC ACID
PART
9910.0
0.00791
0.05730
258.6
0.00021
0.00089
51.8
0.00004
0.00023
39.6
0.00003
0.00017
SOS
NOX
HC
CO
0.0
0.00000
0.00000
52.4
o.oooot
0.00029
5441.0
0.00*34
0.03030
20.0
0.00002
0.00011
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
56560.0
0.24600
0.18800
0.0
0.00000
0.00000
67.2
0.00063
0.00030
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.3
0.00000
0.00000
2203.0
0.01900
0.00873
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
2721.0
0.00305
0.00279
0.0
0.00000
0.00000
0.0
0.00000
0.00000
2
2
2
2
3
329.1
0.00026
0.00183
15.7
0.00001
0.00009
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
SOURCE
MASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
SURFACE COATING - MAJOR APPLIANCE FINISHING
SURFACE COATING - SHALL APPLIANCE FINISHING
SURFACE COATING - FARM MACHINERY FINISHING
SURFACE COATING - INDUSTRIAL MACHINERY FINISHING
SURFACE COATING - COMMERCIAL MACHINERY FINISHING
SURFACE COATING • WOOD FURNITURE FINISHING
SURFACE COATING » SHEET, STRIP AND COIL COATING
SURFACE COATING - METAL FURNITURE FINISHING
SURFACE COATING - PAPER AND PAPERBOARD COATING
SWIMMING POOL HEATING
SYH-TRIMETHYLENE-TRINITRAMINE
SYNTHETIC RUBBER PRODUCTION - EMULSION POLYMERIZATION
SYNTHETIC RUBBER PRODUCTION - SOLUTION POLYMERIZATION
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
143.6
0.00011
o.oooao
0.0
0.00000
0.00000
609.6
0.00049
0. 00340
67.6
0.00005
0.00036
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
4.5
0.00002
0.00002
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
366.8
0.00535
0.00254
22.7
0.00021
0.00010
0.0
0.00000
0.00000
0.0
0.00000
0.00000
31390.0
0.27000
0.12400
4356.0
0.03750
0.01730
1996.0
0.01720
0.00791
7993.0
0.06680
0.03170
1010.0
0.00069
0.00400
0694.0
0.07660
0.03520
506400.0
4.36000
2.01000
BOS1.0
0.06930
0.03190
499400.0
4.30000
1.98000
60.5
0.00052
0.00024
0.0
0.00000
0.00000
6271.0
0.05400
0.02480
3691.0
0.03180
0.01460
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
151.2
0.00017
0.00015
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
NJ
SOURCE
2»».5-T SALTS
TEPP
TERBACIL
TEREPHTHALIC ACID
TETRAETHYL/TCTRAHETHYL LEAD
TETRACYCLINE
TIN COnPOUNOS - HALIOESi OXIDES. SULFATES, OTHERS
TITANIUM DIOXIDE - PIGMENT
TOBACCO
TOLUENE-2. 4-OIAHINE
TOLUENE
TOLUENE DIISOCYANATE
TOLUENE SULFONIC ACID
MASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1.7
0.00000
0.00001
4278.0
o.oosm
0.02380
79*. 3
0.00063
0.00442
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
1986.0
0.01880
0.00888
0.0
0.00000
0.00000
6937.0
0.06170
0.02920
0.0
0.00000
0.00000
0.0
0.00000
0.00000
4.9
0.00004
0.00002
0.2
0.00000
0.00000
0.7
0.00001
0.00000
367.4
0.00316
0.00146
1188.0
0.01020
0.00471
3.5
0.00003
0.00001
0.0
0.00000
0.00000
0.0
0.00000
0.00000
39710.0
0.34200
0.15700
0.4
0.00000
0.00000
3113.0
0.02680
0.01230
1016.0
0.00875
0.00403
4.1
0.00004
0.00002
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
119100.0
0.13400
0.12200,
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
(71
CO
SOURCE
TOLUENE SULFONATE - HYOROTROPE
TOXAPHENE
TOXAPHENE APPLICATION ON CROPS
TRANSPORT OF SULFUR
TRANSPORT OF ASBESTOS ORE
.TRANSPORT OF SAND AND GRAVEL
TRANSPORT OF CLAY
TRANSPORT OF TALC ORE
TRICHLOROETHYLENE - FROH ACETYLENE
1.1.2-TRICHLOROETHANE - FROM ETHYLENE DICHLORIDE
1.1.1-TRICHLOROETHANE
TRICHLOROETHYLENE - FROH ETHYLENE
TRICHLORFON . DIPTEREX
MASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
3.6
0.00003
0.00001
63.9
O.OOOS5
0.00025
0.0
0.00000
0.00000
0.0
0.00000
0.00000
63.2
0.00005
0.00028
110.7
0.00009
0.00061
84ieo.o
0.06720
0.46900
2506.0
0.00206
0.00867
61.2
0.00005
0.00027
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
64.3
0.00055
0.00025
68.0
0.00059
0.00027
5137.0
0.04420
0.02040
10240.0
0.08820
0.04060
0.3
0.00000
0.00000
0.0
0.00000
0.00000
1.4
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
SOURCE
MASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
2»«».5-TRICHLOROPHENOXY ACETIC ACID ESTERS
TRICHLOROTRIFLUOROETHANE
TRICHLOROPHENOLS
TRIETHYLAM1NE
TRIFLURALIN
TRIHETHYLAH1NE
TRIPLE SUPERPHOSPHATES
UNPAVED ROADS
UREA
VARNISH MANUFACTURERS
VEGETABLE OIL HILLING
VERNOLATE
VINYLIOENE CHLORIDE
0.0
0.00000
0.00000
0.0
0.00000
0.00000
3.7
0.00000
0.00003
0.0
0.00000
0.00000
10.9
0.00001
0.00006
0.0
0.00000
0.00000
338.9
0.00027
0.00189
99990000.0
79.80000
557.00000
1545.0
0.00123
0.00861
0.0
0.00000
0.00000
6464.0
0.00516
0.03600
1.1
0.00000
0.00001
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
14.5
0.00006
0.00005
0.0
0.00000
0.00000
1424.0
0.00619
0. 00473
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
064.9
0.00202
0.0015"*
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
10.9
0.00010
0.00005
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
o.b
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.5
0.00000
0.00000.
6.6
0.00007
0.00003
11. 3
0.00010
0.00004
10.1
0.00009
0.00004
0.0
0.00000
0.00000
13.1
0.00011
0.00005
0.0
0.00000
0.00000
0.0
0.00000
0.00000
18680.0
0.16100
0.07400
3694.0
0.03180
0.01460
3.4
0.00003
0.00001
326.6
0.00281
0.00129
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
SOURCE
MASS OF EMISSIONS (1000 K6/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
Ul
VINYL ACETATE - FROM ETHYLENE
VTNYL ACETATE - FROM ACETYLENE
VINYL BROMIDE
VINYL CHLORIDE - ACETYLENE
VINYL CHLORIDE • ETHYLENE DICHLORIDE
VITAMIN B COMPLEXES
VITAMIN A
VITREOUS KAOLIN PRODUCTS
WET CORN MILLING
WIND EROSION OF SOIL FROM DORMANT LAND
WOOD WASTE INCINERATION
WOOD PROCESSING - KRAFT OR SULFATE PROCESS
WOOD PROCESSING - SULFITE PROCESS
0.0
0.00000
0.00000
32.7
0.00003
0.00018
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
20170.0
0.01610
0.11200
13100.0
0.01050
0.07300
2139000.0
1.71000
6.96000
95820.0
0.07640
0.53400
276000.0
0.22000
1.54000
25040.0
0.02000
0.13900
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
896.6
0.00390
0.00298
0.0
0.00000
0.00000
9382.0
0.04170
0.03180
63720.0
0.26600
0.21800
405100.0
1.76000
1.34000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
224.1
0.00212
0.00100
0.0
0.00000
0.00000
23960.0
0.22600
0.10700
0.0
0.00000
0.00000
0.0
0.00000
0.00000
12060.0
0.10400
0.04790
1198.0
0.01030
0.00475
6.2
0.00009
0.00002
530.7
0.00457
0.00210
10360.0
0.08910
0.04100
4.4
0.00004
0.00002
0.5
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
95820.0
0.82500
0.38000
74130.0
0.63800
0.29400
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
896.6
0,00101
0.00092
0.0
0.00000
0.00000
287500.0
0.32200
0.29500
920100.0
1.03000
0.94500
0.0
0.00000
0.00000
-------
SOURCE
MASS OF EMISSIONS 11000 K6/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
PART
S02
NOX
HC
CO
WOOD PROCESSING - NEUTRAL SULFITE SEMI-CHEMICAL
P-XYLENE
XYLENE SULFONIC ACID
H-XYLENE
XYLENE SULFONATE - SODIUM SALT
0-XYLENE
XYLENE SULFONATE - AMMONIUM SALT
XYLENE SULFONATE - POTASSIUM SALT
ZINC OXIDE - PIGMENT
ZINC GALVANIZING OPERATIONS
ZINC CHROMATE - PIGMENT
ZINC CHLORIDE - SO DEGREE BAUME*
ZINEB
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
7087.0
0.00565
0.03950
1082.0
0.00086
0.0060S
0.3
0.00000
0.00000
32.3
0.00003
0.00018
1.6
0.00000
0.00001
4874.0
0.02120
0.01620
0.0
0.00000
0.00000
0.0
0.00000
0.00000
36.4
0.00016
0.00012
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
650.9
0.00283
0.00216
0.0
0.00000
0.00000
2410.0
0.02280
0.01080
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
3667.0
0.03330
0.01530
1148.0
0.00988
0.00455
8.1
0.00007
0.00003
363.6
0.00313
0.00144
8.5
0.00007
0.00003
5387.0
0.04640
0.02130
1.1
0.00001
0.00000
0.9
0.00001
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
4.8
0.00004
0.00002
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
0.0
0.00000
0.00000
-------
MASS OF EMISSIONS (1000 KG/YR)
PERCENT OF TOTAL INCLUDING METALLURGICAL PROCESSING
SOURCE
PART
S02
NOX
HC
CO
SUB-TOTAL SOURCE ASSESSMENT DATA BASE
OPEN SOURCE WITHHELD EMISSION DATA
TOTAL SOURCE ASSESSMENT DATA BASE -
123000000.0 22960000.0 10590000.0 11620000.0 69190000.0
2326000.0
125300000.0 22960000.0 10590000.0 11620000.0 69190000.0
NEDS TOTALS 1972
17950000.0 30130000.0 22360000.0 29200000.0 97340000.0
-------
REFERENCES
1. National Emissions Report, 1972. EPA-450/2-74-012, U.S. En-
vironmental Protection Agency, Research Triangle Park, North
Carolina. June 1974. 422 pp.
68
-------
.'TECHNICAL REPORT DATA
(Please read Instructions on the reverse before completing/
i. REPORT NO.
EPA-600/2-78-
2.
3. RECIPIENT'S ACCESSION-NO.
4. TITLE AND SUBTITLE
SOURCE ASSESSMENT: Overview Matrix for National
5. REPORT DATE
July 1978
Criteria Pollutant Emissions (1978)
6. PERFORMING ORGANIZATION CODE
7. AUTHOR(S)
E. C. Einratis, R. P.Quill, and G. M. Rinaldi
8. PERFORMING ORGANIZATION REPORT NO.
MRC-DA-796
9. PERFORMING ORGANIZATION NAME AND ADDRESS
Monsanto Research
1515 Nicholas Road
Dayton, Ohio 45407
ion
10. PROGRAM ELEMENT NO.
1AB015; ROAP 21AXM-
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: 3-7/78
14. SPONSORING AGENCY CODE
EPA/600/13
15. SUPPLEMENTARY NOTES 1ERL-RTP project officer is Dale Ao Denny, Mail Drop 62,
919/541-2547. Related reports are in the EPA-600/2-76-032 and -77-107'
series. EPA-600/2-77-107c was the previous report.
16. ABSTRACT
repOFjj. alphabetically lists stationary sources that emit criteria pol-
lutants. The overview matrix was prepared using a computerized data base esta-
blished for emissions of air pollutants from approximately 800 stationary source
types in the combustion, organic materials, inorganic materials, and open source
categories. The matrix lists the total national emissions of criteria pollutants emit-
ted by source type. (A source type is defined as a group of emission sources which
have the same process and emission characteristics. )
KEY WORDS AND DOCUMENT ANALYSIS
DESCRIPTORS
b.lDENTIFIERS/OPEN ENDED TERMS
c. COSATI Field/Group
Air Pollution
Assessments
Industrial Processes
Combustion Products
Organic Compounds
Inorganic Compounds
Air Pollution Control
Stationary Sources
Source Assessment
Criteria Pollutants
Open Sources
13B
13H
21B
07C
07B
3. DISTRIBUTION STATEMENT
Unlimited
19. SECURITY CLASS (ThisReport)
Unclassified
21. NO. OF PAGES
77
20. SECURITY CLASS (Thispage)
Unclassified
22. PRICE
EPA Form 2220-1 (9-73)
69
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