United States
Environmental Protection
Agency
Office of Air Quality
Planning and Standards
Research Triangle Park NC 27711
EPA-450M-89-022
November 1989
Air
&EPA
PMio EMISSION FACTOR LISTING
DEVELOPED BY
TECHNOLOGY TRANSFER
AND
AIRS SOURCE CLASSIFICATION
CODES
WITH DOCUMENTATION
-------
EPA-450/4-89-022
PMio EMISSION FACTOR LISTING
DEVELOPED BY
TECHNOLOGY TRANSFER
AND
AIRS SOURCE CLASSIFICATION
CODES
WITH DOCUMENTATION
By
Engineering Science
Cary.NC 27511
EPA Contract No. 68-02-4398
EPA Project Officer Archibald A. MacQueen
Office Of Air Quality Planning And Standards
Office Of Air And Radiation
U. S. Environmental Protection Agency
Research Triangle Park, NC 27711
November 1989
-------
This report has been reviewed by the Office Of Air Quality Planning And Standards, U. S. Environmental
Protection Agency, and has been approved for publication as received from the contractor. Approval does
not signify that the contents necessarily reflect the views and policies of the Agency, neither does mention
of trade names or commercial products constitute endorsement or recommendation for use.
EPA-450/4-89-022
-------
TABLE OF CONTENTS
Page
Introduction 1
Key to PM1Q Emission Factors 2
LISTING:
External Combustion Boilers 3
External Combustion Space Heaters 5
Internal Combustion Engines 5
Chemical Manufacturing 8
Food And Agriculture 11
Primary Metal Production 12
Secondary Metal Production 19
Mineral Products 23
Petroleum Industry 29
Wood Products 30
Fabricated Metal Products 31
Oil And Gas Production 31
Printing 32
Surface Coating 32
Solid Waste Disposal 32
APPENDIX, Documentation 35
111
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AIRS SOURCE CLASSIFICATION CODES
PM10 EMISSION FACTOR LISTING
TECHNOLOGY TRANSFER
INTRODUCTION
This document supplements the second edition of the "NEDS
Source Classification Codes and Emission Factor Listing - PM,Q"
published in August, 1988. A companion document provides SCC/
emission factor data on other air pollutants (SOx, NOx, VOC, CO,
PM): AIRS Facility Subsystem Source Classification Codes And
Emission Factor Listing For Criteria Air Pollutants, EPA-450/4-
90-003, March 1990.
These documents support the EPA-required annual reporting by
states of the emissions of pollutants for which EPA has
established National Ambient Air Quality Standards (NAAQS). The
Source Classification Codes (SCCs) are those required for storing
source and emissions data in EPA's AIRS Facility Subsystem (AFS),
and in States'computerized source files. The emission factors
are default values, provided by EPA for use when the preferred
source-specific values are not available to the reporting agency.
The PM1Q emission factors in this document have been
compiled by technology transfer, in which a PM,Q source not yet
characterized by a PM1Q emission factor is related by engineering
judgement to a similar source with established PM,Q and PM
emission factors. The PM1Q weight percent of the Known source's
PM emissions is applied to the PM emission factor of the similar
source to be characterized. No judgement of the accuracy of the
PM1Q emission factors produced by this process is attempted.
Sucn PM1Q emission factors are, however, considered to be
approximately as accurate as default estimates. Documentation
for emissions factors presented in this document is provided in
the Appendix.
PM and PM1Q emission factor data used in this technology
transfer process are derived from the information in the
following three EPA publications: (1) Compilation of Air
Pollutant Emission Factors. AP-42. fourth edition, through
Supplement A, October 1986 and Supplement B, September 1988; (2)
Gap-Filling PM,Q Emission Factors for Selected Open Area Dust
Sources. EPA-450/4-88-003. February 1988, and (31 Criteria
Pollutant Emission Factors for the 1985 NAPAP Emissions
Inventory. EPA/600/7-87/015, May 1987. Comments or questions on
the emission factors should be addressed to the Criteria
Emissions Section (MD-14), Office of Air Quality Planning and
Standards, U.S. Environmental Protection Agency, Research
Triangle Park, North Carolina, 27711. The telephone number is
(919) 541-5575 (FTS 629-5575).
-------
Key to PM1Q Emission Factors
1. An "A" accompanying an emission factor means that this factor
is the weighted average ash content of the fuel burned, expressed
as a percent. See, for example, SCC 1-01-008-01 on the facing
page. If the weighted average ash content of the coke burned
were five percent (5%), then the emission factor would become 7.9
x 5 or 39.5 pounds of PM1Q emitted (before control) per ton of
coke burned.
2. An "S" accompanying an emission factor means that this factor
is the weighted average sulfur content of the fuel burned,
expressed as a percent. See, for example, SCC 3-10-004-02 on
page 31. If the weighted average sulfur content of the residual
oil burned were three percent (3%), then the emission factor
would become 10.3 x 3 or 30.9 pounds of PM10 emitted (before
control) per one thousand gallons of residual oil burned.
3. The entry " " means that as yet we have no emission factor
for this SCC. See, for example, SCC 1-01-002-17 on the facing
page.
4. The "Reference Number", in the column on the right side of
the listing, identifies the respective emission factor
documentation, given in the appendix.
-------
AIRS SOURCE CLASSIFICATION CODES AND PM,0 EMISSION FACTOR
LISTING BY TECHNOLOGY TRANSFER
Page
Number*
SCC
Process
Factor Units
Ibs/unit
Reference
Number
EXTERNAL COMBUSTION BOILERS - ELECTRIC GENERATION - 4911
6
6
Bituminous Coal
1-01-002-17 - Atmospheric
Fluid Bed
Process Gas (Specify Gas in Comments^
1-01-007-01 - Boilers Over 3.0
100 MMBtu/Hr
1-01-007-02 - Boilers under 3.0
100 MMBtu/hr
Coke
1-01-008-01 - All Boiler 7.9A
Sizes
Liquified Petroleum Gas (LPG^
1-01-010-01 - Butane 0.28
1-01-010-02 - Propane 0.26
Bagasse
1-01-011-01 - All Boiler 5.6
Sizes
Liquid Waste
1-01-013-02 - Waste Oil 12.5
Tons Burned
106 Cu. Ft.
Burned
106 Cu. Ft.
Burned
Tons Burned
103 Gal. Burned
103 Gal. Burned
Tons Burned
103 Gal. Burned
5
6
8
EXTERNAL COMBUSTION BOILERS - INDUSTRIAL
Anthracite Coal
1-02-001-07 - Hand-Fired
Process Gas
1-02-007-01 - Petroleum
Refinery Gas
5.2
3.0
Tons Burned
106 Cu. Ft.
Burned
10
*In the second edition of "NEDS Source Classification Codes and Emission Factor Listing - PM10",
fed August, 1988.
-------
Page SCC Process PM10 Reference^^
Number Factor Units Number ^^
Ibs/unit
6
6
8
8
8
8
8
8
8
8
Coke
1-02-008-02 - All Boiler 5.5A
Sizes
1-02-008-04 - Cogeneration 5.5A
Wood/Bark Waste
1-02-009-03 - Wood-Fired 7.9
Boiler (Greater than 50,000
LB Steam)
1-02-009-06 - Wood-Fired 7.9
Boiler (Less than 50,000
LB Steam)
Liquified Petroleum Gas CLPG)
1-02-010-01 - Butane 0.28
1-02-010-02 - Propane 0.26
Bagasse
1-02-011-01 - All Boiler 5.6
Sizes
CO Boiler
1-02-014-01 - Natural Gas 3.0
1-02-014-02 - Process Gas 3.0
EXTERNAL COMBUSTION BOILERS - COMMERCIAL
Anthracite Coal
1-03-001-03 - Hand-Fired 5.2
Bituminous Coal
Tons Burned
Tons Burned
Tons Burned
Tons Burned
103 Gal.
Burned
103 Gal.
Burned
Tons Burned
106 Cu. Ft.
Burned
106 Cu. Ft.
Burned
/INSTITUTIONAL
Tons Burned
11
12
13
14
15
' 16
1
17
18
19
20
1-03-002-14 - Hand Fired
1-03-002-17 - Atmospheric
Fluid Bed
7.8
Tons Burned
Tons Burned
21
21b
-------
Page SCC Process PM1Q
Number Factor
Ibs/unit
Wood/Bark Waste
9 1-03-009-03 - Wood-Fired 7
Boiler
Liquid Petroleum Gas CLPG)
9 1-03-010-01 - Butane 0
9 1-03-010-02 - Propane 0
EXTERNAL COMBUSTION - SPACE HEATERS
Industrial Space Heaters
10 1-05-001-05 - Distillate Oil 1
10 1-05-001-06 - Natural Gas 3
10 1-05-001-10 - Liquified 1
Petroleum Gas (LPG)
Commercial Space Heaters
10 1-05-002-05 - Distillate Oil i
10 1-05-002-06 - Natural Gas 3
10 1-05-002-09 - Wood 25
10 1-05-002-10 - Liquified 1
Petroleum Gas (LPG)
INTERNAL COMBUSTION ENGINES - ELECTRIC
Distillate Oil ( Diesel)
10 2-01-001-01 - Turbine 4
10 2-01-001-02 - Reciprocating 32
Natural Gas
10 2-01-002-01 - Turbine 14
10 2-01-002-02 - Reciprocating 10
Kerosene /Naphtha (Jet Fuel)
Reference
Units Number
. 9 Tons Burned
.28 103
.26 103
-e&5 2.*K> 103
.0 106
.85 103
r*#5 2. V^IO3
.0 106
Gal
Gal
Gal
Cu.
Gal
Gal
Cu.
. Burned
. Burned
. Burned
Ft . Burned
. Burned
. Burned
Ft . Burned
.0 Tons Burned
.85 103
GENERATION
.8 103
.0 103
.0 106
.0 106
Gal . Burned
- 4911
Gal
Gal
Cu.
Cu.
. Burned
. Burned
Ft . Burned
Ft . Burned
22
23
24
25
26
27
28
29
30
31
32
33
34
35
10
2-01-009-01 - Turbine
4.8
103 Gal. Burned
36
-------
Page
Number
sec
Process
«.
Factor
Ibs/unit
Units
Reference
Number
10
2-01-009-02 - Reciprocating 32.0
103 Gal. Burned
37
INTERNAL COMBUSTION - INDUSTRIAL
Distillate Oil fDiesel
10
10
10
10
10
10
11
11
11
2-02-001-01 -
2-02-001-02 -
2-02-001-03 --
Cogeneration
2-02-001-04 -
Cogeneration
Natural Gas
2-02-002-01 -
2-02-002-02 -
2-02-002-03 -
Cogeneration
2-02-002-04 -
Cogeneration
Gasoline
2-02-003-01 -
Turbine
Reciprocating
Turbine :
Reciprocating :
Turbine
Reciprocating
Turbine:
Reciprocating
Reciprocating
4
32
4
32
14
10
14
10
6
.8
.0
.8
.0
.0
.0
.0
.0
.2
10
10
10
10
10
10
10
10
10
Larcre Bore Enctine
11
11
11
11
11
11
2-02-004-01 -
2-02-004-02 -
(Oil/Gas)
2-02-004-03 -
( Cogeneration )
Diesel
Dual Fuel
Dual Fuel
Residual /Crude Oil
2-02-005-01 - Reciprocating
Kerosene /Naphtha CJet Fuel}
2-02-009-01 -
2-02-009-02 -
Turbine
Reciprocating
46
2
0
30
4
32
.0
.0
.032
.8
.8
.0
10
10
10
10
10
10
3
3
3
3
6
6
6
6
3
3
3
5
3
3
3
Gal.
Gal.
Gal.
Gal.
Cu.
Cu.
Cu.
Cu.
Gal.
Gal.
Burned
Burned
Burned
Burned
Ft . Burned
Ft . Burned
Ft . Burned
Ft . Burned
Burned
Burned
HP-Hours
Brake HP-Hours
Gal.
Gal.
Gal.
Burned
Burned
Burned
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
-------
Page SCC Process PM10
Number Factor
Ibs/unit
11
11
11
11
11
11
11
11
11
11
11
11
11
Liquified Petroleum Gas (LPG)
2-02-010-01 - Propane: 5.0 103
Reciprocating
2-02-010-02 - Butane: 5.0 103
Reciprocating
INTERNAL COMBUSTION - COMMERCIAL/INSTITUTIONAL
Distillate Oil (Diesell
2-03-001-01 - Reciprocating 32.0 103
2-03-001-02 - Turbine 4.8 103
Natural Gas
2-03-002-01 - Reciprocating 10.0 106
2-03-002-02 - Turbine 14.0 106
Gasoline
2-03-003-01 - Reciprocating 6.2 103
Liquified Petroleum Gas (LPG)
2-03-010-01 - Propane: 5.0 103
Reciprocating
2-03-010-02 - Butane: 5.0 103
Reciprocating
INTERNAL COMBUSTION - ENGINE TESTING
Aircraft
2-04-001-01 - Turbojet 11.3 103
2-04-001-02 - Turboshaft 11.3 103
Turbine
2-04-003-01 - Natural Gas 14.0 106
2-04-003-02 - Diesel/Kerosene 4.8 103
Reciprocating
Reference
Units Number
Gal . Burned
Gal . Burned
Gal . Burned
Gal . Burned
Cu. Ft. Burned
Cu. Ft. Burned
Gal . Burned
Gal . Burned
Gal . Burned
Gal. Fuel
Gal. Fuel
Cu . Ft . Burned
Gal . Burned
53
54
55
56
57
58
59
60
61
62
63
64
65
12
2-04-004-01 - Gasoline
6.2
10 Gal. Burned
66
-------
Page
Number
SCC
Process
Factor
Ibs/unit
Units
Reference'
Number
12
2-04-004-02 - Diesel/Kerosene 32.0
103 Gal. Burned
67
CHEMICAL MANUFACTURING - MAJOR GROUP 28
AdJPJC Acid - 2869
12
12
12
12
12
3-01-001-01 - General
3-01-001-05 - Apidic Acid
Refining
3-01-001-06 - Adipic Acid
Drying/Loading and Storage
Ammonia Production — 2873
3-01-003-06 - Primary
Reformer: Natural Gas Fired
3-01-003-07 - Primary
0
0
0
0
0
.037
.004
.032
.144
.86
Tons
Tons
Tons
Tons
Tons
of Product
of Product
of Product
Produced
Produced
68
69
70
71
72
Reformer: Oil Fired
Carbon Black Production - 2895
12 3-01-005-03 - Gas Furnace 3.2
Process (Main Process Vent)
12 3-01-005-04 - Oil Furnace 6.53
Process (Main Process Vent)
12 3-01-005-06 - Transport Air 0.58
Vent
12 3-10-005-07 - Pellet Dryer 0.45
12 3-01-005-08 - Bagging/Loading 0.06
12 3-01-005-09 - Furnace Process 0.2
Fugitive Emissions
Charcoal Manufacture - 2861
13 3-01-006-03 - Batch Kiln 255.4
13
3-01-006-04 - Continuous
Furnace
255.4
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
74
75
76
77
78
79
80
81
13
3-01-006-05 - Briquetting
24.1
Tons Produced
82
8
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Page
Number
SCC
Process
«.
Factor
Ibs/unit
Units
Reference
Number
13
13
13
14
14
14
14
15
15
15
15
16
16
16
Explosives - Trinitrotoluene - 2892
3-01-010-15 - Batch Process: 23.5
Red Water Incinerator
3-01-010-23 - Continuous 0.24
Process: Red Water
Incinerator
3-01-010-30 - Open Burning:
Waste
Phosphoric Acid: Thermal Process - 2874
3-01-017-03 - Absorber w/ 2.14
Packed Tower
3-01-017-04 - Absorber w/ 2.53
Venturi Scrubber
3-01-017-05 - Absorber w/ 0.69
Glass Mist Eliminator
3-01-017-06 - Absorber w/ 5.46
Wire Mist Eliminator
3-01-017-07 - Absorber w/ 0.11
High-pressure Mist Eliminator
3-01-017-08 - Absorber w/ 1.66
Electrostatic Precipitator
Tons Produced 83
Tons Produced 84
Tons TNT Burned 85
Tons P205 Produced 86
Tons P205 Produced
Tons P205 Produced
Tons P205 Produced
Tons P205 Produced
Tons P205 Produced
Plastics Production - Specific Products - 2821
3-01-018-01 - Polyvinyl 23.0
Chlorides & Copolymers
3-01-018-02 - Polypropylene 2.0
and Copolymers
Phthalic Anhydride - 2865
3-01-019-02 - o-Xylene 12.2
Oxidation: Pre-treatment
3-01-019-06 - Naphthalene 4.7
Oxidation: Pre-treatment
Printing Ink Manufacturer - 2893
3-01-020-05 - Pigment Mixing
Tons Product
Tons Product
Tons Produced
Tons Produced
Tons Pigment
87
88
89
90
91
92
93
94
95
96
-------
Page SCC Process
Number
16
16
16
18
18
18
18
18
18
18
18
18
18
18
18
Sodium Carbonate — 2812
3-01-021-02 - Solvay:
Handling
3-01-021-06 - Rotary Dryer:
Gas-Fired
3-01-021-14*- Rotary Dryer:
Steam Tube
Ammonium Nitrate Production —
3-01-027-04 - Neutralizer
3-01-027-08 - Pan Granulator
3-01-027-09 - Bulk Loading
(General)
3-01-027-10 - Bagging Product
3-01-027-11 - Neutralizer
(High Density)
3-01-027-12 - Prilling Tower
(High Density)
3-01-027-14 - Prill Coolers
(High Density)
3-01-027-17 - Evaporator/
Concentrator (High Density)
3-01-027-18 - Coating
(High Density)
3-01-027-21 - Neutralizer
(Low Density)
3-01-027-27 - Evaporator
Concentrator (Low Density)
3-01-027-28 - Coating (Low
Density)
PM1Q Reference
Factor Units Number
Ibs/unit
10.5
17.6
14.0
2873
4.35
0.05
— . —
4.35
3.0
0.01
0.49
3.4
4.35
0.49
3.4
Tons Produced
Tons Product
Tons Product
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
97
98a
98b
99
100
101
102
103
104
105
106
107
108
109
110
* New SCC
10
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Page SCC Process PM1Q
Number Factor
Ibs/unit
20
20
20
20
20
20
20
21
21
21
21
21
21
21
21
25
35
Inorganic Picrments — 2816
3-01-035-01 - Titanium Ti02 27.6
Sulfate Process: Calciner
3-01-035-06 - Lead Oxide: 0.64
Barton Pot
3-01-035-07 - Lead Oxide: 15.0
Calcining Furnace
3-01-035-10 - Red Lead 1.0
3-01-035-15 - White Lead 0.69
3-01-035-20 - Lead Chromate
3-01-035-51 - Ore Dryer 6.9
Urea Production - 2873
3-01-040-02 - Solution 0.011
Concentration (Controlled)
3-01-040-03 - Prilling 3.57
3-01-040-04 - Drum Granulation 4.82
3-01-040-05 - Solid Product: 3.4
Coating
3-01-040-05 - Solid Product:
Bagging
3-01-040-07 - Bulk Loading
Lead Alkyl Manufacture — ( Sodium/Lead
3-01-042-01 - Recovery 59.3
Furnace
3-01-042-04 - Sludge Pits
Ammonium Sulfate — 2873
3-01-130-05 - Fluid Bed Dryer 21.8
Instant Coffee Products - 2095
3-02-003-01 - Spray Dryer 0.93
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Alloy
Tons
Tons
Tons
Tons
Reference
Units Number
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Process 1 - 2869
Produced
Produced
Produced
Green Beans
111
112
113
114
115
116
117
118
119
120
121
122
123
124
125
126
127
-------
Page SCC
Number
Cotton Ginni
35 3-02-004-01
35 3-02-004-02
Process
,na - 0724
- Unloading Fan
- Seed Cotton
PM1Q Reference
Factor Units Number
Ibs/unit
Bales of Cotton 128
Bales of Cotton 129
35
35
35
36
36
36
36
38
38
40
40
Cleaning System
3-02-004-03 - Stick/Burr
Machine
3-02-004-04 - Miscellaneous
(Lint Cleaner/Battery Conden-
sers/Master Trash/Overflow/
Mote Fans)
3-02-004-10 - General
(Entire Process, Alternative
to Above)
Feed and Grain Country Elevators - 5153
3-02-006-08 - Elevator Legs 0.23
fHeadhouse)
Bales of Cotton
Bales of Cotton
130
131
Bales of Cotton
4221
132
3-02-006-11 - Elevator Legs 0.7
(Headhouse)
Rve Milling - 2041
3-02-007-24 - Millhouse 42.7
Wheat Mills - 2041
3-02-007-34 - Millhouse 42.7
Fish Processing - 2077. 2091
3-02-012-05 - Steam Tube Dryer 1.05
Tons Grain
Processed
Tons Grain
Shipped or
Received
133
134
3-02-012-06 - Direct Fire
Dryer
1.68
Tons Grain Received 135
Tons Grain Received 136
Tons Fish Scrap 137
Tons Fish Scrap 138
Aluminum Ore - Bauxite - 1051
3-03-000-02 - Drying Oven 0.70
Aluminum Ore: Electro-Reduction - 3334
Tons of Ore
139
3-03-001-01 - Prebaked
Reduction Cell
54.5
Tons of Molten 140
Aluminum Produced
12
-------
Page
Number
SCC
Process
*
Factor
Ibs/unit
Units
Reference
Number
40 3-03-001-04 - Materials 5.8
Handling
41 3-03-001-10 - Vertical Stud 3.70
Soderberg: Fugitive Emis.
Aluminum Hydroxide Calcining - 3334
41 3-03-002-01 - Overall Process 24.0
By-Product Coke Manufacturing - 3312
41 3-03-003-08 - Oven/Door Leaks 0.48
41 3-03-003-10 - Coal Crushing 0.05
41 3-03-003-12 - Coke Crushing/ 0.04
Screening/Handling
41 3-03-003-14 - Topside Leaks 0.08
Coke Manufacture: Beehives - 3312
41 . 3-03-004-01 - General 97.8
Primary Copper Smelters - 3331
41 3-03-005-02 - Multiple 23.8
Hearth Roaster
41 3-03-005-05 - Fire (Furnace) 9.2
Refining
41 3-03-005-06 - Ore Concen- 4.8
trate Dryer
41 3-03-005-07 - Reverberatory 13.5
Smelting Furnace with Ore
Charging (w/o Roasting)
41 3-03-005-09 - Fluidized Bed 29.2
Roaster
42 3-03-005-10 - Electric 58.0
Smelting Furnace
42 3-03-005-12 - Flash Smelting 83.0
Tons of Molten 141
Aluminum Produced
Tons of Molten 142
Aluminum Produced
Tons of Alumina 143
Produced
Tons Coal Charged 144
Tons Coal Processed 145
Tons Coke Processed 146
Tons Coal Charged 147
Tons Coal Charged 148
Tons Concentrated 149
Ore Processed
Tons Concentrated 150
Ore Processed
Tons Concentrated 151
Ore Processed
Tons Concentrated 152a
Ore Processed
Tons Concentrated 152b
Ore Processed
Tons Concentrated 153
Ore Processed
Tons Concentrated 154
Ore Processed
13
-------
Page
Number
sec
Process
Factor
Ibs/unit
Units
Reference
Number
42
42
42
42
42
42
42
42
42
42
42
3-03-005-13 - Roasting:
Fugitive Emissions
3-03-005-14 - Reverberatory
Furnace: Fugitive Emissions
3-03-005-15 - Converter:
Fugitive Emissions
3-03-005-16 - Anode Refining
Furnace: Fugitive Emissions
3-03-005-17 - Slag Cleaning
Furnace: Fugitive Emissions
3-03-005-22 - Slag Cleaning
Furnace
3-03-005-23 - Reverberatory
Furnace w/Convertor
3-03-005-25 - Fluid Bed
Roaster w/Reverberatory
Furnace and Converter
3-03-005-26 - Concentrate
Dryer w/Electric Furnace &
Cleaning Furnace & Converter
3-03-005-27 - Concentrate
Dryer w/Flash Furnace &
Converter
3-03-005-28 - Noranda Reactor
and Converter
1.4
0.17
2.6
0.46
7.7
9.6
13.5
29.2
4.8
4.8
Tons Concentrated 155
Ore Processed
Tons Concentrated 156
Ore Processed
Tons Concentrated 157
Ore Processed
Tons Concentrated 158
Ore Processed
Tons Concentrated 159
Ore Processed
Tons Concentrated 160
Ore Processed
Tons Concentrated 161
Ore Processed
Tons Concentrated 163
Ore Processed
Tons Concentrated 164a
Ore Processed
Tons Concentrated 164b
Ore Processed
Tons Concentrated 164c
Ore Processed
42
42
3-03-005-29 - Multiple Hearth 23.8
Roaster w/Reverberatory Furnace
& Converter
3-03-005-30 - Fluid Bed
Roaster w/Electric Furnace
& Converter
29.2
Tons Concentrated 164d
Ore Processed
Tons Concentrated 164e
Ore Processed
14
-------
Page
Number
SCC
Process
*
Factor
Ibs/unit
Units
Reference
Number
42
42
42
42
42
3-03-005-31 - Reverberatory 13.5
Furnace after Multiple Hearth
Roaster
3-03-005-32 - Reverberatory 13.5
Furnace after Fluid Bed
Roaster
3-03-005-33 - Electric Fur- 58.0
nace after Concentrate Dryer
3-03-005-34 - Flash Furnace 83.0
after Concentrate Dryer
3-03-005-35 - Electric 58.0
Furnace after Fluid Bed
Roaster
Tons Concentrated 164f
Ore Processed
Tons Concentrated 164g
Ore Processed
Tons Concentrated 164h
Ore Processed
Tons Concentrated 164i
Ore Processed
Tons Concentrated 164j
Ore Processed
42
42
43
43
43
43
43
Ferroalloy (Open Furnace) - 3313
3-03-006-02 - 75% Ferro- 199
silicon: Elec. Smelting
Furnaces
3-03-006-03 - 90% Ferro- 355
silicon: Elec. Smelting
Furnaces
Tons Produced
Tons Produced
Ferroalloy (Semi-covered Furnace) - 3313
3-03-007-01 - Ferromanganese: 3*&Gr }£>.$ Tons Produced
Electric Arc Furnace
Iron Production - 3312
3-03-008-01 - Blast Furnace: 41.8
Ore Charge
3-03-008-02 - Blast Furnace: 15.2
Agglomerates Charge
Sintering - 3312
3-03-008-14 - Sinter Discharge 1.02
End
165
166
167
3-03-008-17 - Sinter Cooler
0.45
Tons Iron Produced 168
Tons Iron Produced 169
Tons Sinter
Produced
Tons Sinter
Produced
170
171
15
-------
Page SCC Process PM1Q Referenc^p
Number Factor Units Number ^^
Ibs/unit
43
43
44
3-03-008-19 - Sinter 0.12
Processing (Combined Code
Includes 15, 16, 17, 18)
3-03-008-20 - Sinter Con- 0.013
veyor: Transfer Station
3-03-008-26 - Blast Furnace 33.0
Slips
Steel Production - 3312
Tons Sinter
Produced
Tons Sinter
Transferred
Number of Slips
172
173
174
44 3-03-009-04 - Electric Arc 6.55
Furnace: Stack (Alloy Steel)
44 3-03-009-08 Electric Arc 29.0
Furnace: Stack (Carbon
Steel)
44 3-03-009-13 - Basic Oxygen 13.1
Furnace: Open Hood - Stack
44 3-03-009-14 - Basic Oxygen 13.1
Furnace: Closed Hood - Stack
44 3-03-009-15 - Hot Metal 0.09
(Iron) Transfer to Steel-
making Furnace
44 3-03-009-21 - Teeming 0.03
(Unleaded Steel)
45 3-03-009-25 - Teeming 0.36
(Leaded Steel)
45 3-03-009-32 - Machine Scarfing 0.1
Lead Smelters - 3332
45 3-03-010-05 - Materials 4.25
Handling (Includes 11,12,
13,04,14)
45 3-03-010-06 - sintering: 181.0
Dual Stream Feed End
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons of Lead
Processed
Tons of
Concentrated
Ore Processed
175
176
177
179
180
181
182
183
184
16
-------
Page
Number
SCC
Process
Factor
Ibs/unit
Units
Reference
Number
45 3-03-010-08 - Slag Fume 1.29
Furnace
45 3-03-010-09 - Lead Dressing 0.47
45 3-03-010-10 - Crushing & 0.85
Grinding
45 3-03-010-11 - Raw Material 0.34
Unloading
45 3-03-010-12 - Raw Material 0.26
Storage Piles
45 3-03-010-13 - Raw Material 0.43
Transfer
45 3-03-010-14 - Sintering 1.90
Charge Mixing
45 3-03-010-15 - Sinter 0.12
Crushing/Screening
45 3-03-010-16 - Sinter Transfer 0.015
45 3-03-010-17 - Sinter Fines 4.8
Return Handling
45 3-03-010-19 - Blast Furnace 0.07
Tapping (Metal and Slag)
45 3-03-010-20 - Blast Furnace 0.93
Lead Pouring
45 3-03-010-21 - Blast Furnace 0.13
Slag Pouring
45 3-03-010-22 - Lead Refining/ 1.76
Silver Retort Building
45 3-03-010-23 - Lead Casting 0.85
45 3-03-010-24 - Reverberatory 2.94
or Kettle Softening
Tons of Lead
Processed
Tons of Lead
Processed
Tons Processed
Tons of Raw
Material
Tons of Raw
Material
Tons of Raw
Material
Tons of Raw
Material
Tons of Sinter
Tons of Sinter
Tons of Sinter
Tons of Lead
Product
Tons of Lead
Product
Tons of Lead
Product
Tons of Lead
Product.
Tons of Lead
Product
Tons of Lead
Product
185
186
187
188
189
190
191
192
193
194
195
196
197
198
199
200
17
-------
Page SCC Process
Number
45
45
46
46
46
46
46
46
46
46
46
46
46
46
3-03-010-25 - Sinter Machine
Leakage
?MI(V
Factor
Ibs/unit
0.67
3-03-010-26 - Sinter Dump Area 0.0008
Titanium Processina - 3339, 3369. 3356
3-03-012-02 - Drying
Titanium Sand Ore (Cyclone
Exit)
Taconite Iron Ore Processina
3-03-023-04 - Ore Transfer
3-03-023-07 - Bentonite
Storage
3-03-023-12 - Indurating
Furnace: Gas Fired
3-03-023-13 - Indurating
Furnace: Oil Fired
3-03-023-14 - Indurating
Furnace: Coal Fired
3-03-023-21 - Haul Road:
Rock
0.43
- 1011
0.085
0.03
24.8
24.8
24.8
6.2
3-03-023-22 - Haul Road: 5.2
Taconite
Metal Mininci — General Processes — 1011
3-03-024-01 - Primary
Crushing (low moisture ore)
3-03-024-02 - Secondary
Crushing (low moisture ore)
3-03-024-03 - Tertiary
Crushing (low moisture ore)
3-03-024-04 - Material
0.05
0.10
0.16
0.06
Reference!
Units Number
Tons of Sinter
Tons of Sinter
Tons Processed
Tons Pellets
Produced
Tons Pellets
Produced
Tons Pellets
Produced
Tons Pellets
Produced
Tons Pellets
Produced
Vehicle-Miles
Traveled
Vehicle-Miles
Traveled
-1099
Tons Ore Processed
Tons Ore Processed
Tons Ore Processed
Tons Ore Processed
201
202
203
204
205
206
207
208
209
210
211
212
213
214
Handling (low moisture ore)
18
-------
Page
Number
SCC
Process
*
Factor
Ibs/unit
Units
Reference
Number
47
47
47
47
47
47
47
47
47
47
47
48
48
48
48
3-03-024-05 - Primary
Crushing (high moisture ore)
3-03-024-06 - Secondary
Crushing (high moisture ore)
3-03-024-07 - Tertiary
Crushing (high moisture ore)
3-03-024-08 - Material
Handling (high moisture ore)
3-03-024-09 - Dry Grinding
w/air conveying
3-03-024-10 - Dry Grinding
w/o air conveying, etc.
3-03-024-11 - Ore Drying
Zinc Smelting - 3339
3-03-030-09 - Raw Material
Handling and Transfer
0.009 Tons Ore Processed 215
0.02 Tons Ore Processed 216
0.02 Tons Ore Processed 217
0.005 Tons Ore Processed 218
20.2 Tons Ore Processed 219
2.35
12.0
3.4
Tons Ore Processed 220
Tons Ore Processed 221
3-03-030-10 - Sinter Breaking 1,
and Cooling
Tons Processed
Tons Processed
222
223
3-03-030-11
3-03-030-12
Unloading
Secondary
- Zinc
- Raw
Cooper
Casting
Material
Smeltina
2.1
0.23
and Al
Tons
Tons
lovinci
Processed
Processed
( Brass /Bronze
224
225
Melt}
33AJLJJ362
3-04-002-07 - Scrap Dryer 253.0
(Rotary)
3-04-002-08 - Wire Burning 253.0
(Incinerator)
Tons of Charge
Tons of Charge
Cupolas
3-04-002-10 - Charge w/
Scrap Copper
0.00027 Tons of Charge
3-04-002-11 - Charge w/ 211.6
Insulated Copper Wire
Tons of Charge
226
227
228
229
19
-------
Page
Number
SCC
Process
Factor
Ibs/unit
Units
Reference'
Number
48
48
48
48
48
49
49
49
49
49
49
49
49
49
49
49
3-04-002-12 - Charge w/
Scrap Copper and Brass
64.4
Reverberatory Furnace
3-04-002-14 - charge w/Copper 5.1
3-04-002-15 - Charge w/ 21.2
Brass and Bronze
Rotary Furnace
3-04-002-17 - Charge w/ 177
Brass and Bronze
Crucible and Pot Furnaces
3-04-002-19 - Charge w/ 12.4
Brass and Bronze
Electric Arc Furnace
3-04-002-20 - Charge w/Copper 5.0
3-04-002-21 - Charge w/Brass 6.5
and Bronze
Electric Induction Furnace
3-04-002-23 - Charge w/Copper 7.0
3-04-002-24 - Charge w/Brass 20.0
and Bronze
Fugitive Emissions
3-04-002-31 - Scrap Dryer
8.2
3-04-002-32 - Wire Incinerator 8.2
3-04-002-33 - Sweating Furnace 0.45
3-04-002-34 - Cupola Furnace 2.2
3-04-002-35 - Reverberatory 3.1
Furnace
3-04-002-36 - Rotary Furnace 2.6
3-04-002-37 - Crucible Furnace 0.29
Tons of Charge
Tons of Charge
Tons of Charge
Tons of Charge
Tons of Charge
Tons of Charge
Tons of Charge
Tons of Charge
Tons of Charge
Tons of Charge
Tons of Charge
Tons of Charge
Tons of Charge
Tons of Charge
Tons of Charge
Tons of Charge
230
231
232
233
234
235
236
237
238
239
240
241
242
243
244
245
20
-------
Page
Number
SCC
Process
Factor
Ibs/unit
Units
Reference
Number
49
49
49
49
49
49
49
49
49
49
49
49
49
50
50
50
50
3-04-002-38 - Electric 0.08
Induction Furnace
3-04-002-39 - Casting 0.015
Operations
Gray Iron Foundries - 3321
3-04-003-02 - Reverberatory 1.7
Furnace
3-04-003-03 - Electric 0.86
Induction Furnace
3-04-003-15 - Charge Handling 0.36
3-04-003-20 - Pouring/Casting 2.8
3-04-003-25 - Casting Cooling 1.4
3-04-003-40 - Casting Grind- 1.7
ing/Cleaning
3-04-003-50 - Sand 0.54
Grinding/Handling
3-04-003-51 - Core Ovens 2.22
3-04-003-52 - Sand Grinding/ 6.0
Handling
3-04-003-53 - Core Ovens 0.90
3-04-003-60 - Castings 0.0045
Finishing
Secondary Lead Smelting - 3341. 3369
3-04-004-01 - Pot Furnace 0.2
Reverberatory 194
3-04-004-02
Furnace
3-04-004-03
(Cupola)
3-04-004-04
Furnace
- Blast Furnace 129
- Rotary Sweating 64
Tons of Charge 246
Tons of Casting 247
Produced
Tons Metal Charged 248
Tons Metal Charged 249
Tons Metal Charged 250
Tons Metal Charged 251
Tons Metal Charged 252
Tons Metal Charged 253
Tons Sand Handled 254
Tons Sand Handled 255
Tons Metal Charged 256
Tons Metal Charged 257
Tons Metal Charged 258
Tons Metal Charged 259
Tons Metal Charged 260
Tons Metal Charged 261
Tons Metal Charged 262
21
-------
Page
Number
sec
Process
Factor
Ibs/unit
Units
Number
50
50
50
50
50
50
50
50
50
50
50
51
51
51
51
3-04-004-05 - Reverberatory
Sweating Furnace
31
3-04-004-08 - Barton Process 40.0
Reactor (Oxidation Kettle)
3-04-004-09 - Casting 0.87
3-04-004-12 - Sweating
Furnace: Fugitive
3-04-004-13 - Smelting
Furnace: Fugitive
3-04-004-14 - Kettle
Refining: Fugitive
2.35
10.0
0.002
Lead Battery Manufacture - 3691
3-04-005-05 - Overall
Process 125
3-04-005-07 - Paste Mixing
3.92
3-04-005-10 - Lead Reclaiming 1.67
Furnace
3-04-005-11 - Small Parts 0.19
Casting
3-04-005-12 - Formation 32.4
Steel Foundry - 3324. 3325
3-04-007-03 - Open Hearth 8.5
Furnace with Oxygen Lance
3-04-007-05 - Electric 0.09
Induction Furnace
3-04-007-06 - Sand Grinding/ 0.54
Handling in Mold and Core
Making
3-04-007-07 - Core Ovens 2.22
Tons Metal Charged 263
Tons Lead 264
Oxide Produced
Tons of Lead Cast 265
Tons Metal Charged 266
Tons Metal Charged 267
Tons Metal Charged 268
103 Batteries
Produced
103 Batteries
Produced
103 Batteries
Produced
103 Batteries
Produced
103 Batteries
Produced
Tons Metal
Processed
Tons Metal
Processed
Tons Sand
Processed
Tons Sand
Processed
269
270
271
272
273
274
275
276
277
22
-------
Page SCC Process PM10
Number Factor
Ibs/unit
51
51
51
51
51
51
51
3-04-007-08 - Pouring and &*V £.£
Casting
3-04-007-11 - Castings 1.7
Cleaning
3-04-007-12 - Charge 0.36
Handling
3-04-007-13 - Casting U^=6 1.4
Cooling
3-04-007-15 - Finishing: 0.0045
Specify in Comments
3-04-007-16 - Sand Grinding 6.0
and Handling
3-04-007-17 - Core Ovens 0.90
Lead Cable Coatina - 3357. 3315
53 3-04-040-01 - General 0.36
MINERAL PRODUCTS - MAJOR GROUPS 11. 12. 14. 28
54
54
54
54
Asphalt Roofing Manufacture - 2952
3-05-001-01 - Asphalt 6.8
Blowing: Saturant
3-05-001-02 - Asphalt 25.0
Blowing: -Coating
3-05-001-03 - Felt 0.5
Saturation: Dipping Only
3-05-001-04 - Felt Satu- 2.26
Reference
Units Number
Tons Metal
Processed
Tons Metal
Processed
Tons Metal
Processed
Tons Metal
Processed
Tons Metal
Processed
Tons Metal
Processed
Tons Metal
Processed
Tons Lead
Processed
. 29. 32. 44
Tons Asphalt
Processed
Tons Asphalt
Processed
Tons Asphalt
Shingle
Tons Asphalt
278
279
280
281
282
283
284
285
286
287
288
289
54
54
ration: Dipping/Spraying
Asphaltic Concrete - 2951
3-05-002-02 - Hot Elevators
Screens, Bins & Mixer
0.03
3-05-002-03 - Storage Piles 0.12
Shingle
Tons Produced
Tons Produced
290
291
23
-------
Page
Number
SCC
Process
*
Factor
Ibs/unit
Units
Referencei
Number
54
54
55
55
55
55
55
55
55
55
3-05-002-04 - Cold Aggregate
Handling
0.04
55
55
55
55
3-05-002-11 - Rotary Dryer - 0.36
Conventional Plant, w/cyclone
Brick Manufacturing - 3251
3-05-003-01 - Raw Material
Drying
3-05-003-03 - Storage of
Raw Materials
3-05-003-08 - Screening
3-05-003-11 - Curing and
Firing: Gas-Fired
3-05-003-12 - Curing and
Firing: Oil-Fired Tunnel
Kilns
3-05-003-14 - Curing and
Firing: Gas-Fired Periodic
Kilns
3-05-003-15 - Curing and
12.0
1.4
0.01
0.32
0.034
0.47
Firing: Oil-Fired Periodic Kilns
3-05-003-16 - Curing and 10.0
Firing: Coal-Fired Periodic
Kilns
Calcium Carbide - 2819
3-05-004-01 - Electric 22.0
Furnace (Hoods & Main Stack)
3-05-004-02 - Coke Dryer 1.0
3-05-004-03 - Furnace Room 24.0
Vents
Castable Refractory - 3255
3-05-005-05 - Molding and 20.0
Shakeout
Tons Produced
Tons Produced
292a
292b
Tons Raw Material 293
Tons Material 294
Stored
Tons Raw Material 295
Tons Produced 296
Tons Brick Produced 297
Tons Produced
Tons Produced
Tons Produced
298
299
300
Tons Produced
Tons Produced
Tons Produced
301
302
303
Tons Feed Material 304
24
-------
Page
Number
SCC
Process
Factor
Ibs/unit
Units
Reference
Number
Cement Manufacturing - Drv Process - 3241
56
56
56
56
56
56
56
56
56
56
56
56
56
56
56
3-05-006-07 - Raw Material
Unloading
0.1
1.4
3-05-006-08 - Raw Material
Piles
3-05-006-09 - Primary Crushing 0.26
3-05-006-10 - Secondary 1.13
Crushing
3-05-006-12 - Raw Material 0.15
Transfer
3-05-006-19 - Cement Load Out 0.20
Wet Process - 3241
3-05-007-07 - Raw Material 0.1
Unloading
3-05-007-08 - Raw Material 1.4
Piles
3-05-007-09 - Primary Crushing 0.26
1.13
3-05-007-10 - Secondary
Crushing
3-05-007-12 - Raw Material
Transfer
0.15
Tons Material
Tons in Piles
Tons Processed
Tons Processed
Tons Handled
Tons Cement
Produced
Tons of Material
Unloaded
Tons in Piles
Tons Processed
Tons Processed
Tons Handled
Tons Cement
Produced
305
306
307
308
309
310
311
312
313
314
315
316
3-05-007-19 - Cement Loadout 0.20
Clav and Flv Ash Sintering CLow Density Aggregate Manufacture1) - 3295
3-05-009-03 - Natural Clay/ 6.12
Shale Sintering
3-05-009-04 - Raw Clay/Shale 0.25
Crushing/Screening
3-05-009-05 - Raw Clay/Shale 0.40
Transfer/Conveying
Tons Finished
Product
317
Tons Raw Material 318
Tons Raw Material 319
25
-------
Page SCC
Number
57
57
57
57
57
57
57
58
Surface Mini
3-05-010-21
Removal
3-05-010-22
3-05-010-23
3-05-010-30
3-05-010-33
Drilling
3-05-010-34
Drilling
3-05-010-37
Overburden
3-05-010-42
Process PM1Q
Factor
Ibs/unit
na Operations - 1111. 1211
- Overburden
- Drilling/Blasting
- Loading 0.05
- Topsoil Removal
- Overburden: 0.16
- Coal Seam: 0.028
- Truck Loading: 0.015
- Truck 0.001
Reference
Units Number
Tons Coal Mined
Tons Coal Mined
Tons Coal Mined
Tons Topsoil
Removed
Holes Drilled
Holes Drilled
Tons Overburden
Loaded
Tons Overburden
320
321
322
323
324
325
326
327
58
58
58
Unloading: Bottom Dump-
Overburden
3-05-010-43 - Open Storage. 17,060
Pile: Coal
3-05-010-48 - Overburden 0.006
Replacement
3-05-010-49 - Wind Erosion: 380
Exposed Areas
Acres Coal 328
Storage Area
Tons Overburden 329
Acres Exposed Area 330
59
Concrete Batching - Fugitive Emissions - 3271. 3272. 3273. 3275
1771. 3292
3-05-011-20 - Asbestos/Cement 0.1
Products
Tons Produced
331
Wool-Type Glass Fiber - 3296
59 3-05-012-01 - Regenerative 20.7
Furnace
59 3-05-012-02 - Recuperative 25.9
Furnace
Tons Material
Processed
Tons Material
Processed
332
333
26
-------
Page SCC
Number
59 3-05-012-03 -
Furnace
59 3-05-012-04 -
(Rotary Spun)
59 3-05-012-05 -
(Rotary Spun)
59 3-05-012-06 -
59 3-05-012-07 -
Furnace
Process PM10 Reference
Factor Units Number
Ibs/unit
Electric 0.47
Forming
Curing Oven 9 . 0
Cooling 1.3
Unit Melter 8.6
59 3-05-012-08 - Forming
(Flame Attenuation)
59 3-05-012-09 - Curing 6.0
(Flame Attenuation)
Textile-Type
59 3-05-012-11 -
Furnace
59 3-05-012-12 -
Furnace
59 3-05-012-13 -
Furnace
59 3-05-012-14 -
Process
59 3-05-012-15 -
Glass Fiber - 3229
Regenerative 15.0
Recuperative 1 . 9
Unit Melter 5.7
Forming
Curing 1 . 2
Tons Material
Processed
Tons Material
Processed
Tons Material
Processed
Tons Material
Processed
Tons Material
Processed
Tons Material
Processed
Tons Material
Processed
Tons Material
Processed
Tons Material
Processed
Tons Material
Processed
Tons Material
Processed
Tons Material
334
335
336
337
338
339
340
341
342
343
344
345
59
59
59
Oven
Frit Manufacture - 2899
3-05-013-01 - Rotary Furnace 15.0
Glass Manufacture - 3211. 3221. 3229
Processed
Tons Charged
346
3-05-014-03 - Flat Glass:
Melting Furnace
1.9
3-05-014-04 - Pressed and 16.5
Blown Glass: Melting Furnace
Tons Glass Produced 347
Tons Glass Produced 348
27
-------
Page
Number
SCC
Process
*
Factor
Ibs/unit
Units
Reference
Number
Gypsum Manufacture - 3275
60 3-05-015-04 - Conveying 0.15
60 3-05-015-05 - Primary 0.26
Crushing: Gypsum Ore
60 3-05-015-06 - Secondary 1.13
Crushing: Gypsum Ore
60 3-05-015-21 - End Sawing 6.80
(8 Ft)
60 3-05-015-22 - End Sawing 4.25
(12 Ft)
Lime Manufacture — 3274
60 3-05-016-01 - Primary 0.26
Crushing
60 3-05-016-02 - Secondary 1.13
Crushing/Screening
60 3-05-016-03 - Calcining- 5.00
Vertical Kiln dd
60 3-05-016-05 - Calcimatic 31.5
Kiln d
-------
Page
Number
SCC
Process
*
Factor
Ibs/unit
Units
Reference
Number
61
61
61
61
Phosphate Rock - 1475
3-05-019-04 - Open Storage 14.4
Stone Quarrvina/Processina - 1411. 1422
Tons Phosphate Rock 364
. 1423. 1429. 1499
3-05-020-06 - Miscellaneous
Operation-Screen/Convey/
Handling
3-05-020-07 - Open Storage 0.12
3-05-020-09 - Blasting -
General
61 3-05-020-12 - Drying
Sand/Gravel - 1442. 1446
62 3-05-025-02 - Aggregate
Storage
62 3-05-025-03 - Material
Transfer & Conveying
62 3-05-025-07 - Storage
Piles
5.0
0.12
1,367.0
Tons Raw Material 365
Tons Product Stored 366
Tons Raw Material 367
Tons Stone Dryed 368
Tons Product
0.0064 Tons Product
369
370
Acres of Storage 371
Area
PETROLEUM INDUSTRY - MAJOR GROUP 29
Petroleum Process Heaters 2911
66 3-06-001-03 - Oil Fired 7.4 S
66
3-06-001-04 - Gas Fired
66 3-06-001-05 - Natural Gas-
Fired
66 3-06-001-06 - Process Gas-
Fired
66
3-06-001-07 - LPG Fired
3.0
3.0
3.0
0.27
103 Gallons Oil
Burned
106 Cubic Feet
Burned
106 Cubic Feet
Burned
106 Cubic Feet
Burned
10 Gallons Burned
372
373
374
375
376
29
-------
Page SCC Process PM10 Reference)
Number Factor Units Number
Ibs/unit
66
66
68
69
69
69
70
70
70
70
70
70
70
Fluid Catalytic Crackincr Units (
3-06-002-01 - Fluid 169
Catalytic Cracking Unit
3-06-003-01 - Thermal Cat- 11
alytic Cracking Unit
Fluid Cokina Units - 2911
3-06-012-01 - Fluid Coking 366
Units
Sulfate (Kraft^ Puloina - 2611.
Industrial Boilers')
3-07-001-08 - Fluid Bed 50
Calciner
FCC1
.4
.9
.0
2621
.4
3-07-001-10 - Recovery 230.0
Furnace/Indirect Contact
Evaporator
Pulpboard Manufacture - 2631, 2661
3-07-004-02 - Fiberboard: 0
General
Plywood/Particleboard Operations
3-07-007-01 - General: 2
Not Classified
3-07-007-03 - Particleboard 0
Drying
3-07-007-04 - Waferboard 498
Dryer
3-07-007-11 - Fir-Sapwood- 2
Steam Fired
3-07-007-12 - Fir-Sapwood- l
Gas-Fired
3-07-007-13 - Fir-Heartwood 1
Plywood Veneer dryer
3-07-007-14 - Larch 2
- 2911
10J BBLs. Fresh Feed
103 BBLs. Fresh Feed
103 BBLs. Fresh Feed
. 2631 (For Bark Boilers
Air-Dry Tons
Unbleached Pulp
Air-Dry Tons
Unbleached Pulp
.35 Tons Finished
Product
- 2435. 2436. 2492
.47
.35
.0
.69
.37
.84
.40
10* Sq. Ft. 3/8"
Plywood
Tons Processed
104 LBs. Waf /Chips
Dried
104 Sq. Ft. 3/8"
Plywood
104 Sq. Ft. 3/8"
Plywood
104 Sq. Ft. 3/8"
Plywood
104 Sq. Ft. 3/8"
377
378
379
. See
380
381
382
383
384
385
386
387
388
389
Plywood Veneer dryer
Plywood
30
-------
Page
Number
70
70
70
70
70
70
70
70
70
SCC Process
3-07-007-15 - Southern Pine
Plywood Veneer dryer
Sawmill Operations - 2421,
3-07-008-01 - Log Debarking
3-07-008-02 - Log Sawing
3-07-008-03 - Sawdust Pile
Handling
PM10
Factor
Ibs/unit
2.15
2426, 2429
0.011
0.20
0.36
3-07-008-04 - Sawing: Cyclone 0.90
Exhaust
3-07-008-05 - Planing/
Trimming: Cyclone Exhaust
3-07-008-06 - Sanding:
Cyclone Exhaust
3-07-008-07 - Sanderdust:
Cyclone Exhaust
3-07-008-08 - Other
Cyclones : Exhaust
0.90
2.00
2.50
0.80
Miscellaneous Woodworkina Ooerations -
71
71
74
2439
3-07-030-01 - Wood Waste
Storage Bin Vent
3-07-030-02 - Wood Waste
Storage Bin Loadout
Drum Cleanina/Reclamation -
3-09-025-01 - Drum Burning
Furnace
Oil & Gas Production - Fuel
Process Heaters
0.58
1.20
5085
0.02
Fired Equi
Reference
Units Number
104 Sq. Ft. 3/8"
Plywood
Tons of Logs
Processed
Tons of Logs
Processed
Tons of Sawdust
SCFM Average
Airflow
SCFM Average
Airflow
SCFM Average
Airflow
Hours of Operation
Hours of Operation
2421. 2426. 2429. 2431
Tons Wood Waste
Tons Wood Waste
Drums Burned
pment
390
391
392
393
394
395
396
397
398
. 2434.
399
400
401
76
3-10-004-01 - Distillate Oil 1.0
103 Gal. Burned
402
31
-------
Page SCC
Number
76 3-10-004-02
76 3-10-004-03
76 3-10-004-04
76 3-10-004-05
Process
- Residual Oil
- Crude Oil
- Natural Gas
- Process Gas
Steam Generators
76 3-10-004-11 - Distillate Oil
76 3-10-004-12
76 3-10-004-13
76 3-10-004-14
76 3-10-004-15
Typesettina
- Residual Oil
- Crude Oil
- Natural Gas
- Process Gas
(Lead Remeltinal
!>*
Factor
Ibs/unit
10
10
3
3
1
10
10
3
3
.33
.33
.0
.0
.0
.33
.33
.0
.0
103
10
10
10
10
10
10
10
10
3
6
6
3
3
3
6
6
Units
Gal
Gal
Cu.
Cu.
Gal
Gal
Gal
Cu.
Cu.
Reference
Number
. Burned
. Burned
Ft.
Ft.
Burned
Burned
. Burned
. Burned
. Burned
Ft.
Ft.
Burned
Burned
403
404
405
406
407
408
409
410
411
- 2791
79
85
3-60-001-01 - Remelting 0.18
(Lead Emissions Only)
Tons Melted
412
Surface Coating of Automobiles and Light Trucks - 3711. 3713
4-02-016-01 - Prime
Application, Electrodepo-
sition/Dip/Spray
6.40
Tons Solvent
in Coating
413
SOLID WASTE DISPOSAL GOVERNMENT
106
106
106
106
106
Other Incineration
5-01-005-05 - Pathological
5.92
5-01-005-07 - Conical Design 11.0
(Tee Pee) Municipal Refuse
5-01-005-08 - Conical Design 3.85
(Tee Pee) Wood Refuse
5-01-005-10 - Trench 4.94
Burner: Wood
5-01-005-11 - Trench 52.4
Burner: Tires
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
414
415
416
417
418
32
-------
Page SCC Process PM10 Reference
Number Factor Units Number
Ibs/unit
106
SOLID
107
107
107
107
107
107
107
107
SOLID
5-01-005-12 - Trench 14.1 Tons Burned
Burner: Refuse
WASTE DISPOSAL - COMMERCIAL /INSTITUTIONAL
Incineration — General
5-02-001-01 - Multiple chamber 4.70 Tons Burned
5-02-001-02 - Single Chamber 5.70 Tons Burned
5-02-001-03 - Controlled Air 1.04 Tons Burned
5-02-001-04 - Conical 11.0 Tons Burned
Design: Municipal Refuse
5-02-001-05 - Conical 3.85 Tons Burned
Design: Wood Refuse
Apartment Incineration
5-02-003-01 - Flue Fed 11.4 Tons Burned
5-02-003-02 - Flue Fed 4.02 Tons Burned
(With Afterburner and Draft
Controls)
Incineration ( Special Purpose)
5-02-005-05 - Pathological 5.92 Tons Burned
Waste
WASTE DISPOSAL - INDUSTRIAL
Incineration
419
420
421
422
423
424
425
426
427
107
107
107
107
107
5-03-001-01 - Multiple Chamber 4.70
5-03-001-02 - Single Chamber 5.70
5-03-001-03 - Controlled Air 1.04
5-03-001-04 - Conical
Design:.Refuse
5-03-001-05 - Conical
Design: Wood Refuse
11.0
3.85
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
428
429
430
431
432
33
-------
Page SCC Process PM10 Reference
Number Factor Units Number
Ibs/unit
107
108
108
108
5-03-001-06 - Trench Burner: 4.94 Tons Burned
Wood
5-03-001-07 - Trench Burner: 52.4 Tons Burned
Tires
5-03-001-08 - Auto Body 1.2 Tons Burned
Components
5-03-001-09 - Trench Burner: 14.1 Tons Burned
433
434
435
436
Refuse
Opening Burning
108 5-03-002-04 - Coal Refuse &O&& O,
-------
APPENDIX
PM10 EMISSION FACTOR DOCUMENTATION
35
-------
36
-------
Documentation
AIRS SOURCE CLASSIFICATION CODES AND
PM1Q EMISSION FACTOR LISTING BY
TECHNOLOGY TRANSFER
Reference
Number SCC PM Factor- Basis for PM1Q Derivation
1. 1-01-002-17 - No basis for technology transfer.
2. 1-01-007-01 3.0 As stated in AP-42, Section
1.4, all PM from natural gas
combustion is < 1 urn; assume
100% PM < 10 urn.
3. 1-01-007-02 3.0 Same as Ref. *2, 1-01-007-01.
4. 1-01-008-01 10.OA Use AP-42, Appendix C.2, Category
2, which shows, on average, 79%
of PM is < 10 urn.
5. 1-01-010-01 0.28 As stated in Section 1.4, AP42,
all PM from NG combustion is
less than 1 urn: assume same for
LPG.
5. 1-01-010-02 0.26 Same as Ref. =5. 1-01-010-01.
7. 1-01-011-01 16.0 Assume bagasse combustion is
similar to wood bark, for which
AP42, Table 1.6-2 reports 35%
of PM < 10 urn.
8. 1-01-013-02 19.0 Fine Particle Emissions
Information System (FPEIS)
Reports 205 & 207 give data on
crude oil fired industrial
boilers, showing 66% of PM < 10
urn.
9. 1-02-001-07 10.0 Per Section 1.2, AP42, use data
for travel ing grate stoker; Table
1.2-4 states 52% PM < 10 urn.
10. 1-02-007-01 3.0 Same as Ref. #5, SCC
1-01-010-01.
aUnless otherwise noted, particulate matter (PM) factors are taken from Criteria
Pollutant Emission Factors for the 1985 NAPAP Emissions Inventory, EPA/600/7-
87/015, May 1987. Many of these factors are published in USEPA's Compilation
of Air Pollutant Emission Factors. AP-42.
37
-------
Reference
Number
11.
12.
13.
14.
15.
16.
17.
18.
19.
20.
21.
22.
23.
24.
25.
sec
1-02-008-02
1-02-008-04
1-02-009-03
1-02-009-06
1-02-010-01
1-02-010-02
1-02-011-01
1-02-014-01
1-02-014-02
1-03-001-03
1-03-002-14
1-03-009-03
1-03-010-01
1-03-010-02
1-05-001-05
PM Factor
7.0A
7.0A
8.8
8.8
0.28
0.26
16.0
3.0
3.0
10.0
15.0
8.8
0.28
0.26
2.50
26.
27.
1-05-001-06
1-05-001-10
3.0
1.85
Basis For PM10 Derivative
Same as Ref. #4, SCC
1-01-008-01.
Same as Ref. #4, SCC
1-01-008-01.
Use 90% < 10 urn, per
footnote C, Table 1.6-3, AP42.
Same as Ref. #13, SCC
1-02-009-03.
Assume particle size
distribution (psd) is same as
NG: 100% < 10 urn
Same as Ref. #15,
SCC 1-02-010-01
Same as Ref #7,
SCC 1-01-011-01
Same as Ref. ?2, 1-01-007-01
Same as Ref. =18, 1-02-014-01
Same as Ref. #9,
SCC 1-02-001-07
Assume bituminous coal similar
to anthracite; psd same as Ref.
#9, SCC 1-02-001-07
Same as Ref. #13,
SCC 1-02-009-03
Same as Ref. #15,
SCC 1-02-010-01
Same as Ref. #16,
SCC 1-02-010-02
Assume psd is
< 10 urn.
& %> , fro m
Same as Ref. #5, P "
SCC 1-01-010-01
Assume psd from LPG combustion
is same as NG; Ref. #5,
SCC 1-01-010-01
/ n
38
-------
Reference
Number
28.
29.
30.
31.
32.
33.
34.
35.
36.
37.
38.
39.
40.
41.
sec
1-05-002-05
1-05-002-06
1-05-002-09
1-05-002-10
2-01-001-01
2-01-001-02
2-01-002-01
2-01-002-02
2-01-009-01
2-01-009-02
2-02-001-01
2-02-001-02
2-02-001-03
2-02-001-04
PM Factor
2.50
3.0
25.0
1.85
5.0
33.5
14.0
10.0
5.0
33.5
5.0
33.5
5.0
33.5
Basis For PM10 Derivative
Assume same as Ref. #25,
SCC 1-05001-05
Assume same as Ref. 327,
SCC 1-05001-10
AP-42 Section 1.10 notes that
95% of wood smoke particles are
less than 0.4 urn. Assume 100%
<10 urn.
Same as Ref. #18,
SCC 1-02-014-01
From AP-42, App. C.2, Table
C.2-2, use 96% < 10 urn.
From AP-42, App. C.2 Table
C.2-2, use 96% < 10 urn.
Same as Ref. #5,
SCC 1-01-010-01
Same as Ref. ?5,
SCC 1-01-010-01
From App. C.2, Category 1, 96%
< 10 urn.
Same as Ref. #36,
SCC 2-01-009-01
Same as Ref. #32,
SCC 2-01-001-01
Same as Ref. #33,
SCC 2-01-001-02
Same as Ref. #32,
SCC 2-01-001-01
Same as Ref. =33,
SCC 2-01-001-02
42.
43.
44.
2-02-002-01
2-02-002-02
2-02-002-03
14.0
10.0
14.0
Same as Ref. #5,
SCC 1-01-010-01
Same as Ref. #5,
SCC 1-01-010-01
Same as Ref. #5,
SCC 1-01-010-01
39
-------
Reference
Number
45.
46.
47.
48.
49.
50.
51.
52.
53.
54.
55.
56.
57.
58.
59.
60.
61.
sec
2-02-002-04
2-02-003-01
2-02-004-01
2-02-004-02
2-02-004-03
2-02-005-01
2-02-009-01
2-02-009-02
2-02-010-01
2-02-010-02
2-03-001-01
2-03-001-02
2-03-002-01
2-03-002-02
2-03-003-01
2-03-010-01
2-03-010-02
PM Factor
10.0
6.47
50.0
2.2
0.035
33.5
5.0
33.5
5.0
5.0
33.5
5.0
10.0
14.0
6.47
5.0
5.0
Basis For PM10 Derivative
Same as Ref. #5,
SCC 1-01-010-01
. From AP-42, Table C.2-2,
Category 1, assume 96% < 10 urn.
Assume 92% < 10 urn, per Table
C.2-2, since large bore may tend
toward less efficient
combustion, producing more
large particles.
Same as Ref. #47,
SCC 2-02-004-01
Same as Ref. #47,
SCC 2-02-004-01
Same as Ref. #47,
SCC 2-02-004-01
Same as Ref. #47
Same as Ref. #36
Same as Ref. #5,
SCC 1-01-010-01
Same as Ref. #5,
SCC 1-01-010-01
Same as Ref. #33,
SCC 2-01-001-02
Same as Ref. #32, 2-01-001-01
Same as Ref. #5,
SCC 1-01-010-01
Same as Ref. #5,
SCC 1-01-010-01
From AP42, C.2-2, Category 1,
assume psd = 96% < 10 urn
Same as Ref. #5,
SCC 1-01-010-01
Same as Ref. #5,
SCC 1-01-010-01
40
-------
Reference
Number
62.
63.
64.
65.
66.
67.
68.
69.
70.
71.
72.
73.
74.
75.
76.
77.
78.
79.
sec
2-04-001-01
2-04-001-02
2-04-003-01
2-04-003-02
2-04-004-01
2-04-004-02
3-01-001-01
3-01-001-05
3-01-001-06
3-01-003-06
3-01-003-07
3-01-005-01
3-01-005-03
3-01-005-04
3-01-005-06
3-01-005-07
3-01-005-08
3-01-005-09
PM Factor
11.8
11.8
14.0
5.0
6.47
33.5
0.9
0.1
0.8
0.144
0.9
2300.0
3.2
6.53
0.58
0.45
0.06
0.2
Basis For PM10 Derivative
Assume jet engine testing
(firing jet fuel) same as Ref.
#36, SCC 2-01-009-01, Turbine
-(96% < 10 urn)
Same as Ref. #36,
SCC 2-01-009-01
Same as Ref. #2,
SCC 1-01-007-01
From AP-42, Appendix C.2-2,
Category 1, 96% < 10 urn.
Same as Ref. #46,
SCC 2-02-003-01
Same as Ref. #65,
SCC 2-04-004-02
Assume psd is similar to that
of potassium chloride drying,
without controls, as given in
AP-42, App C.l-28; 4.07%
< 10 urn
Same as ?68
Same as #68
Assume pm emissions are from NG
combustion; psd same as Ref.
#46, SCC 2-02-003-01
Assume pm from oil firing, same
as Ref. # 46; 96% < 10 urn.
No plants.
Assume 100% of pm < 10 urn;
AP-42, Section 5.3 states that
all pm is between 10-500 nm
Same as #74
Same as #74
Same as #74
Same as #74
Same as #74
41
-------
Reference
Number
80.
SCC
3-01-006-03
PM Factor
266.0
81.
82.
83.
84.
85.
86.
3-01-006-04
3-01-006-05
3-01-010-15
3-01-010-23
3-01-010-30
3-01-017-03
266.0
56.0
25.0
0.25
180.0
2.14
87.
88.
89.
90.
91.
92.
3-01-017-04
3-01-017-05
3-01-017-06
3-01-017-07
3-01-017-08
3-01-018-01
2.53
0.69
5.46
0.11
1.66
35.0
93,
3-01-018-02
3.0
Basis For PM1Q Derivative
Assume psd similar to coke mfg.:
from AP-42, Table 7.2-2; for
combustion stack, uncon., 96%
< 10 urn.
Same as Ref. #80,
SCC 3-01-006-03
Assume psd similar to coke
pushing, AP-42, Table 7.2-2; 43%
< 10 urn
Assume same as recovery boiler
in pulp mill; 94% < 10 urn
Same as Ref. #83,
SCC 3-01-010-15
No basis for technology transfer
AP42, Section 5.11, Table 2.2
notes that acid mist particle
size is 0.4 - 2.6 urn. Assume
all large particles are
absorbed, and 100% of
particles uncontrolled are
< 10 urn.
Same as Ref. #86,
SCC 3-01-017-03
Same as Ref. #86,
SCC 3-01-017-03
Same as Ref. #86,
SCC 3-01-017-03
Same as Ref. #86,
SCC 3-01-017-03
Same as Ref. #86,
SCC 3-01-017-03
PM emissions from plastics mfg.
generally occur during drying
and post processing. Assume
similar to detergent spray
drying AP-42, Table 5.15-2:
66.1% < 10 urn.
Same as Ref. #92,
SCC 3-01-018-01
42
-------
Reference
Number
94.
95.
96.
97.
98a.
98b.
99.
100.
101.
102.
103.
104.
105.
106.
107.
108.
109.
sec
3-01-019-02
3-01-019-06
3-01-020-05
3-01-021-02
3-01-021-06
3-01-021-14*
3-01-027-04
3-01-027-08
3-01-027-09
3-01-027-10
3-01-027-11
3-01-027-12
3-01-027-14
3-01-027-17
3-01-027-18
3-01-027-21
3-01-027-27
PM Factor
13.0
5.0
2.0
50.0
84.0
67.0
4.35
2.68
0.02
0.19
4.35
3.18
1.6
0.52
4.0
4.35
0.52
Basis For PM10 Derivative
From AP-42, Appendix C-2
Category 9; 94% < 10 urn.
Same as Ref. ?94,
SCC 3-01-018-02
No basis for technology transfer
Assume psd similar to rotary
drying of sodium carbonate, AP-
42, Table 5-16-3; 21% < 10 urn
From AP-42, Section 5.16, Table
5.16-3: 21% < 10 urn
Same as Ref. *98a.
Mostly fume; assume 100% < 10
urn, by engineering judgement.
Assume pan granulator is similar
to rotary-drum granulator;
AP-42, Table 6.8-2; 2% < 10 urn.
No basis for technology
transfer.
No basis
transfer.
for technology
Same as Ref. ?99,
SCC 3-01-027-04
Use prilling from AP-42,
Appendix C.2-2, Category 9; 94%
< 10 urn.
From AP-42, Table 6.8-2, assume
low density prill cooler is same
as high density: 0.4% < urn.
Same as Ref. =104,
SCC 3-01-027-12
From AP-42, App. C.2-2, Category
4, 85% < 10 urn
Same as Ref. #99,
SCC 3-01-027-04
Same as Ref. #104,
SCC 3-01-027-12
*(New Code) Rotary Dryer - Steam Tube
43
-------
Reference
Number
110.
111.
112.
SCC
3-01-027-28
3-01-035-01
3-01-035-06
PM Factor
4.0
230.0
0.64
113.
114.
115.
116.
117.
3-01-035-07
3-01-035-10
3-01-035-15
3-01-035-20
3-01-035-51
15.0
1.0
0.69
0.20
8.0
116.
117.
118.
119.
120.
121.
122.
123.
124.
3-01-035-20
3-01-035-51
3-01-040-02
3-01-040-03
3-01-040-04
3-01-040-05
3-01-040-06
3-01-040-07
3-01-042-01
0.20
8.0
0.021
3.8
241.0
4.0*
0.19
0.02
59.3**
125.
3-01-042-04
1.9
Basis For PM10 Derivative
Same as Ref. #107,
SCC 3-01-027-18
Assume psd similar to lime
calcination; AP-42, Table8.15-
2, where 12% < 10 urn.
100% of lead oxide emissions are
generally < 10 urn, as presented
in AP-42, App. C.I, Section
7.15.
Same as Ref. #112,
SCC 3-01-035-06
Same as Ref. #112,
SCC 3-01-035-06
Same as Ref. #112,
SCC 3-01-035-06
No basis for technology transfer
Assume principal pigment ore
dried is lead, and psd is same
as for storage, AP-42, Section
7.8; 86% < 10 urn.
Assume similar to sodium
carbonate pre-dryer with
controls, AP-42, Table
5.16-3; 52.5% < 10 urn.
Assume psd is as given in
AP-42, Appendix C.2, Category
9; 94% < 10 urn.
Same as Ref. #100,
SCC 3-01-027-08
Same as Ref. #107,
SCC 3-01-027-18
Same as Ref. #101,
SCC 3-01-027-09
Same as Ref. #101,
SCC 3-01-027-09
Lead Oxide (PbO) fume, assumed
to be 100% PMjQ, by engineering
judgement.
No basis for technology transfer
44
-------
Reference
Number
126.
127.
128.
129.
130.
131.
132.
133.
:34.
135.
136.
137.
138.
139.
SCC PM Factor
3-01-130-05 21S.O
3-02-003-01 1.4
3-02-004-01 5.0
3-02-004-02 0.3
3-02-004-03 0.2
3-02-004-04 1.5
3-02-004-10 7.0
3-02-006-08 1.5
3-02-006-11 -i.65
3-02-007-24 70.0
3-02-007-34 70.0
3-02-012-05 5.0
3-02-012-06 8.0
3-03-000-02 1.2
Basis For PM10 Derivative
Assume psd is same as sodium
carbonate fluidized bed dryer,
AP-42, Table 5.16-3; 10%,
'< 10 urn.
Same as Ref. #92,
SCC 3-01-018-01
No basis for technology transfer
No basis for technology transfer
No basis for technology transfer
No basis for technology transfer
No basis for technology transfer
PSD for grain handling in
AP-42, App. C.2, Cat. 6 is used:
15% < 10 urn.
Same as Ref. =133.
SCC 3-02-006-08
From AP-42, App. C.2,
Category 7, 61% < 10 urn.
Same as Ref. # 135,
SCC 3-02-007-24
Assume psd for steam tube dryers
is same as for rotary steam tube
dryer for sodium carbonate,
AP-42, Table 5.16-3; 21% <
10 urn.
Same as Ref. #137,
SCC 3-02-012-05
AP42, Section 7.1 suggests that
psd for miscellaneous fugitive
operations is similar to that
presented in Table 7.1-3, which
shows 58% < 10 urn.
*PM factor from AP-42, Ammonium Nitrate, Table 6.8-1
**The Recovery Furnace emissions are PbO fume. The lead emission factor in AP-
42, 55 Ib (as Pb) was erroneously converted to PbOo, and incorrectly entered
into EPA600/7-87-015 as 63.5 Ib/ton.
45
-------
Reference
Number
140.
141.
142.
143.
144.
145.
146.
sec
147.
148.
149.
150.
151.
152a.
152b.
153.
3-03-001-01
3-03-001-04
3-03-001-10
3-03-002-01
3-03-003-08
3-03-003-10
3-03-003-12
3-03-003-14
3-03-004-01
3-03-005-02
3-03-005-05
3-03-005-06
3-03-005-07
3-03-005-09
3-03-005-10
PM Factor
94.0
10.0
12.0
200.0
0.51
0.11
0.09
0.09
200.0
45.0
10.0
10.0
50.0
55.0
100.0
Basis For PM10 Deriva:ive
Assume psd for prebake cell is
same as that of fugitives, Ref.
139; 58% < 10 urn.
AP42 - Section 7.1 suggests that
psd for fugitives are as shown
in Table 7.1-3; 58% < 10 urn.
Assume psd from VSS fugitives
is same as for HSS, AP-42, Table
7.1-4; 31% < lOum.
Same as Ref. #111,
SCO 3-01-035-01
From AP-42, App. C.2,
Category 9, 94% < 10 urn.
Assume psd for coal crushing is
same as for coal charging, AP-
42, Table 7.2-2; 48.9% < 10 urn.
No basis for technology
transfer. As default value,
assume same as coal crushing;
48.9% < 10 urn.
Same as Ref. *144,
SCC 3-03-003-08
No basis for technology
transfer. As default value, use
psd for coal charging, AP-42,
Table 7.2-2; 48.9% < 10 urn.
Use AP42, Appendix C.2,
Category 5; 53% < 10 urn.
Use AP-42, Appendix C.2-2,
Cat.8; 92% < 10 urn.
As default value, assume psd
similar to Fluorspar drum dryer,
AP-42, App. C.I, C.l-94; 48%
< 10 urn.
From AP-42, Table 7.3-4, 27%
< 10 urn.
Same as Ref. # 149; 53%
< 10 urn.
Assume similar to EAF in steel
refining, AP-42, Table 7.5-2;
58% < 10 urn.
46
-------
Reference
Number SCC
PM Factor
Basis For PM10 Derivative
154.
3-03-005-12
140.0
155.
156.
3-03-005-13
3-03-005-14
2.6
0.4
Fl ash furnace combines roasting
and smelting. Use AP42,
converter, Table 7.3-5; 59% <
10 urn.
Assume psd of fugitives from
roasting are similar to
roasting, Ref. # 149; 53% < 10
urn.
Assume psd of fugitives from
reverberatory furnace are
average from matte tapping
(Table 7.3-7) slag tapping
(Table 7.3-8) and smelter
(Table 7.3-4); 74 + 28 + 27 =
3
43% < 10 urn.
157.
158.
159.
160.
161.
162.
163.
164a
164b
164c
164d
164e
3-03-005-15
3-03-005-16
3-03-005-17
3-03-005-22
3-03-005-23
3-03-005-25
3-03-005-26
3-03-005-27
3-03-005-28
3-03-005-29
3-03-005-30
4.4
0.5
8.0
10.0
36.0
55.0
10.0
10.0
45.0
55.0
Same as Ref. #154,
SCC 3-03-005-12
Same as Ref. =150,
SCC 3-03-005-05
No basis for technology
transfer. As default value, use
psd for fugitive emissions from
converter slag and copper blow,
AP42, Table 7.3-9; 96% < 10 urn.
Same as Ref. #159,
SCC 3-03-005-17
Assume psd same as Ref. #152a;
27% < 10 urn.
Deleted
Same as Ref. #149,
SCC 3-03-005-02; 53% < 10 urn.
Same as Ref. #151,
SCC 3-03-005-06; 48% < 10 urn.
Same as Ref #151; 48% < 10 urn.
No basis for technology
transfer.
Same as Ref. #149; 53% < 10 urn.
Same as Ref. #149; 53% < 10 urn.
47
-------
Reference
Number
SCC
PM Factor
Basis For PM10 Derivative
164f
164g
164h
1641
164j
165.
166.
167.
163.
169.
174.
3-03-005-31
3-03-005-32
3-03-008-01
3-03-008-02
3-03-008-26
50.0
50.0
3-03-005-33 100.0
3-03-005-34 140.0
3-03-005-35 100.0
3-03-006-02 316.0
3-03-006-03 564.0
3-03-007-01 12.0
ilO.O
40.0
170.
171.
172.
173.
3-03-008-14
3-03-008-17
3-03-008-19
3-03-008-20
6.8
3.0
0.8
0.17
87.0
Same as Ref. #152a; 27%
< 10 urn.
Same as Ref. #152a; 27%
< 10 urn.
Same as Ref. #153; 58% < 10 urn.
Same as Ref. #154; 59% < 10 urn.
Same as Ref. #153; 58% < 10 urn.
No basis for technology
transfer. As default value
assume psd is same as for 50%
Si Fe, AP-42, Table 7.4-4; 63%
< 10 urn.
Same as Ref. #165.
Assume same psd
8*% < 10 urn.
-
No basis for technology '
transfer. Assume source of PM
is coke, with psd of 44%
-------
Reference
Number
175.
176.
177.
178.
179.
180.
181.
182.
183.
184.
185.
186.
187.
188.
189.
SCC PM Factor
3-03-009-04 11.3
3-03-009-08
3-03-009-13
3-03-009-14
3-03-009-15
3-03-009-21
3-03-009-25
3-03-009-32
3-03-010-05
3-03-010-06
3-03-010-08
3-03-010-09
3-03-010-10
3-03-010-11
3-03-010-12
50.0
28.5
28.5
0.19
0.07
0.81
0.10
5.0
213.0
4.6
0.48
1.0
0.4
0.3
Basis For PM10 Derivative
Assume similar to carbon steel,
Ap-42, Table 7.5-2; 58%
< 10 urn.
From AP-42, Table 7.5-2, for
electric arc furnace; 58%
< 10 urn.
Assume similar to psd of BOF
charge, AP-42, Table 7.5-2; 46%
< 10 urn.
Same as Ref. #177,
SCC 3-03-009-13
Assume similar to BOF tapping,
AP-42, Table 7.5-2; 45% < 10 urn.
Same as Ref. #179,
SCC 3-03-009-15
Same as Ref. *179,
SCC 3-03-009-15
No basis for technology
transfer. Assume all fume, 100%
< 10 urn, by engineering
judgement.
From AP-42, App. C.2, Category
4, 85% < 10 urn.
Assume same psd as materials
handling, Ref. # 183; 85%
< 10 urn.
No basis for technology
transfer. Assume similar to
psd for copper reverb, furnace
slag tapping; AP-42,
Table 7.3-8; 28% < 10 urn.
Assume psd for process similar
to psd for fugitives from dross
kettle, AP-42, Table 7.6-6; 98%
< 10 urn.
Same as Ref. #183,
SCC 3-03-010-05.
Same as Ref. #183
Same as Ref. #183
49
-------
Reference
Number
190.
191.
192.
193.
194.
195.
196.
197.
198.
199.
200.
201.
202.
203.
204.
205.
206.
207.
sec
3-03-010-13
3-03-010-14
3-03-010-15
3-03-010-16
3-03-010-17
3-03-010-19
3-03-010-20
3-03-010-21
3-03-010-22
3-03-010-23
3-03-010-24
3-03-010-25
3-03-010-26
3-03-012-02
3-03-023-04
3-03-023-07
3-03-023-12
3-03-023-13
PM Factor
0.5
2.26
1.5
0.2
9.0
0.16
0.93
0.47
1.8
0.87
3.0
0.68
0.01
0.5
0.1
0.04
29.2
29.2
Basis For PM10 Derivative
Same as Ref. #183
Assume same psd as fugitive
emissions from lead ore storage;
AP-42, Table 7.6-3; 86% < 10 urn
Same as Ref. #173; 7.74%
< 10 urn.
Same as Ref. #192
Use AP-42, Appendix C.2-2,
Category 5; 53% < 10 urn
Assume similar to BOF tapping,
AP-42, Table 7.5-2; 45% < 10 urn
No basis for technology
transfer. Assume all fume, 100%
< 10 urn based on engineering
judgement.
Same as Ref. =185, 28% < 10 urn
No basis for technology
transfer. Assume psd similar
to fugitives for dross kettle,
Ref. #186; 98% < 10 urn.
Same as Ref. #198.
Same as Ref. #198
Use fugitive psd for sinter
machine, AP-42, Table 7.6-4; 98%
< 10 urn.
Same as Ref. #192; 7.74%
< 10 urn
From AP-42, Appendix C.2,
Category 4; 85% < 10 urn
Assume same psd as fine
crushing; AP-42, App. C.2-2,
Category 4; 85% < 10 urn.
From AP-42, Appendix C.2,
Category 4; 85% < 10 urn.
Same as Ref. #205
Same as Ref. #205
50
-------
Reference
Number
208.
SCC
209.
210.
211
212.
213.
214.
216.
217.
218.
219.
220.
221.
222.
223.
3-03-023-14
3-03-023-21
3-03-023-22
3-03-024-01
3-03-024-02
3-03-024-03
3-03-024-04
3-03-024-05
3-03-024-06
3-03-024-07
3-03-024-08
3-03-024-09
3-03-024-10
3-03-024-11
PM Factor
29.2
11.0
9.3
0.5
1.2
2.7
0.12
0.02
0.05
0.06
0.01
28.8
2.4
19.7
3-03-030-09 4.0
3-03-030-10 1.5
Basis For PM1Q Derivative
Same as Ref. *205
From AP-42, Table 8.22-4;
.Factor: 6.2 Ib/VMT < 10 urn.
From AP-42, Table 8.22-4;
Factor: 5.2 Ib/VMT < 10 urn.
From AP-42, Table 8.23-1;
PMjQ given as 0.05 Ib/ton.
From AP-42, Table 8.23-1 PM1Q
fraction for primary crushing
of low moisture ore is 10%, and
for tertiary, 6%. Assume 8% for
secondary crushing.
Use AP-42, Table 8.23-1.
From AP-42, App. C.2-2,
Category 3, 51% < 10 urn
From AP-42, Table 8.23-1,
for high moisture ore, PMjQ
emission factor is given as
0.009 Ib/ton for primary
grinding.
Same as Ref. #215, for secondary
grinding, 0.02 Ib/ton
Same as Ref. #215, for tertiary
grinding, 0.02 Ib/ton
Same as Ref. # 214
From AP-42, Appendix C-2,
Category 4, low end of range,
70% < urn, assuming air conveying
will increase proportion of
coarse particles in stream.
w/o air conveying; from
AP-42, App.C.2-2 Category 4; 85%
< 10 urn
From AP-42, Table 8.23-1, in
which drying is given as 12.0
or 61% < 10 urn. 19.7
From AP-42, Appendix C.2,
Category 4; 85% < 10 urn.
Same as Ref. 2222.
51
-------
Reference
Number
224.
225.
226.
227.
228.
229.
230.
231.
232.
233.
234.
235.
236.
237.
238.
239.
sec
3-03-030-11
3-03-030-12
3-04-002-07
3-04-002-08
3-04-002-10
3-04-002-11
3-04-002-12
3-04-002-14
3-04-002-15
3-04-002-17
3-04-C02-19
3-04-002-20
3-04-002-21
3-04-002-23
PM Factor
2.5
0.4
275.0
275.0
0.0003
230.0
70.0
5.1
36.0
300.0
21.0
5.0
11.0
7.0
3-04-002-24 20.0
3-04-002-31 13.75
Basis For PM10 Derivative
Same as Ref. #222.
Same as Ref. £141; 58% < 10 urn.
From AP-42, Appendix C.2,
Category 9, 92% < 10 urn
Same as Ref. #226.
Same as Ref. #226.
Same as Ref. #226.
Same as Ref. #226.
Assume similar to SCC
3-04-008-18. Reverb
furnace firing general
metallic scrap; 100% < 10 urn.
Assume similar to secondary
Zn reverb furnace charging
residual metallic scrap,
SCC 3-04-008-38; 59% < 10 urn.
Assume same psd as reverb.
furnace charged with residual
metallic scrap, SCC 3-04-008-
38, 59% < 10 urn
Assume same psd as reverb.
furnace charged with residual
mettalic scrap, SCC 3-04-008-
38, 59% < 10 urn
Assume similar to
SCC 3-04-008-28 Reverb furnace
charged with general
residual metallic scrap, 100%
< 10 um
Assume same psd as reverb.
furnace charged with general
residual metallic scrap, SCC 3-
04-008-38, 59% < 10 um
Assume similar to
SCC 3-04-008-18 Reverb furnace
charged w/scrap; 100% < 10 um
Assume same psd as Ref. #237
Same as Ref. #240; 60% < 10 um
52
-------
Reference
Number SCC PM Factor Basis For PM10 Derivative
240. 3-04-002-32 13.75 Assume psd of all fugitives
similar to SCC 3-04-008-61
through 65; 60% < urn
241. 3-04-002-33 0.75 Assume psd of all fugitives
similar to SCC 3-04-008-61-65;
60% < 10 urn
242. 3-04-002-34 3.66 Assume psd of all fugitives
similar to SCC 3-04-008-61-65;
60% < 10 urn
243. 3-04-002-35 5.27 Assume psd of all fugitives
similar to SCC 3-04-008-61-65;
60% < 10 urn
244. 3-04-002-36 4.43 Assume psd of all fugitives
similar to SCC 3-04-008-61-65;
60% < 10 urn
245. 3-04-002-37 0.49 Assume psd of all fugitives
similar to SCC 3-04-008-61-65;
60% < 10 urn
246. 3-04-002-38 0.14 Assume psd of all fugitives
similar to SCC 3-04-008-61-65;
60% < 10 urn
247. 3-04-002-39 0.015 Assume fugitives from casting
to be 100% < 10 urn, by
engineering judgement
248. 3-04-003-02 2.1 Assume the low range of
AP-42, App. C.2-2 Category 8:
80% < 10 urn
249. 3-04-003-03 0.9 Assume psd to be halfway between
midrange and the high side of
the range of AP-42, App.
C.2-2 Category 8: 95.5% < 10 urn
250. 3-04-003-15 0.6 No basis for technology
transfer. Assume psd same as
fugitives in secondary copper
smelting; 60% < 10 urn
251. 3-04-003-20 2.8 Assume psd same as fugitives
from secondary Zn processing;
100% < 10 urn
252. 3-04-003-25 1.4 Assume psd same as fugitives
from secondary Zn processing;
100% < 10 urn
53
-------
Reference
Number
253.
254.
255.
256.
257.
258.
259.
SCC
260.
261.
262.
3-04-003-40
3-04-003-50
3-04-003-51
3-04-003-52
3-04-003-53
3-04-003-60
3-04-004-01
3-04-004-02
3-04-004-03
3-04-004-03
°M Factor
17.0
3.6*
2.71
40.0
1.1
0.01
0.8
323
307
70.0
263. 3-04-004-05 51.0
264. 3-04-004-08 40.0
Basis For PM1Q Derivative
Assume grinding and cleaning of
castings not to produce more
than 10% < 10 urn PM.
Assume not more than 15%
< 10 urn
Use AP-42, App. C.I, 7.13,
Castings Shakeout; 82% < 10 urn
Same as Ref. #254.
Use AP-42, App. C.I, 7.13,
Castings Shakeout; 82% < 10 urn
Assume psd similar to machine
scarfing in steel production:
45% < 10 urn.
Assume pot furnace similar to
kettle. Psd data in AP-42,
Section 7.11 states median
particle diameter is 18.9 urn.
Assume 25% < 10 urn
In AP-42 Section 7.11,
reverberatory furnaces are
reported as emitting small
particles. Reverb furnace
in AP-42, Section 7.8 produces
60% < 10 urn. Assume same for
lead.
Assume psd relationship for
baghouse - controlled to
uncontrolled - is same as for
blast furnace flue gas to
ventilation; 42% < 10 urn
Assume rotary sweat furnace psd
same as rotary sweat furnace in
secondary Zn (SCC 3-04-008-09);
92% < 10 urn
Assume 60% < 10 urn, as in
SCC 3-04-004-02
From AP-42, Section 7.11, pg.
9, tex states 100% < 10 urn.
* From AP-42, Supplement A, 10/86, Table 7.10-4.
54
-------
Reference
Number SCC PM Factor
265. 3-04-004-09 0.87
266.
267.
268.
269.
270.
271.
272.
273.
274.
3-04-004-12
3-04-004-13
3-04-004-14
3-04-005-05
3-04-005-07
3-04-005-10
3-04-005-11
3-04-005-12
3-04-007-03
2.55
16.5
0.002
139.0
3.92
6.68
0.19
32.4
10.0
275. 3-04-007-05 0.1
276. 3-04-007-06 3.6
Basis For PM10 Derivative
Assume psd same as grid casting
in lead battery mfg.; 100% < 10
urn. From AP-42, Appendix
C.l-65.
Assume psd of fugitives same as
psd of stack emissions (SCC 3-
04-008-09); 92% < 10 urn.
Assume fugitives from smelting
have same psd as Reverb.
furnace, Ref. 260, SCC 3-04-
004-02; 60% < 10 urn.
Assume psd of fugitives from
kettle refining to be 100%
< 10 urn, by engineering
judgement.
Assume psd for overall process
is 90% < 10 urn, since many of
the operations are 100% < 10 urn.
Psd for paste mixing is 100% <
10 urn, per AP-42, App.
C.I - 7.15
Assume similar to pot furnace
in secondary lead processing;
25% < 10 urn
Assume psd for small parts
casting is same as grid casting,
from AP-42, App. C.I - 7.15;
100% < 10 urn.
Assume 100% of pm is sulfuric
acid mist, which AP-42, App.
C.I - 5.17 reports as 100%
< 10 urn
From AP-42, App. C.I - 6.3,
assume psd is similar to psd of
open hearth furnace without 02
lance; 85% < 10 urn
From AP-42, Appendix C.2,
Category 8, 92% < 10 urn.
Same as Ref. #254,
SCC 3-04-003-50
55
-------
Reference
Number SCC
PM Factor
Basis For PM10 Derivative
277.
278.
279.
280.
281.
282.
283.
284.
285.
286.
287.
288.
289.
290.
291.
3-04-007-07
3-04-007-08
3-04-007-11
3-04-007-12
3-04-007-13
3-04-007-15
3-04-007-16
3-04-007-17
3-04-040-01
2.71
3-05-001-01
3-05-001-02
3-05-001-03
3-05-001-04
3-05-002-02
3-05-002-03
17.0
0.6
0.01
40.0
1.1
0.6
7.2
26.7
0.5
3.14
0.2
0.33
Assume psd similar to core oven
in gray iron foundry; 82%
< 10 urn
Assume psd similar to gray iron
foundry; Ref. #251, SCC 3-04-
003-20; 100% < 10 urn
Assume similar to Ref. #253, SCC
304-003-40, gray iron foundry;
10% < 10 urn
Assume psd same as Gray Iron
Foundry, Ref. #250, SCC 3-04-
003-15; 60% < 10 urn.
Same as Ref. #252,
SCC 3-04-003-25; 100% < 10 urn.
Same as Ref. #258,
SCC 3-04-003-60; 45% < 10 urn.
Same as Ref. ?256,
SCC 3-04-003-52, 15% < 10 urn
Same as Ref. #257,
SCC 3-04-003-53; 82% < 10 urn.
Assume same psd as sweating
furnace in sec. lead smelting;
Ref. #263, SCC 3-04-004-05; 60%
< 10 urn
Assume psd similar to
distillation, AP-42, App. C.2,
Category 9, 94% < 10 urn
Same as Ref. #286
Assume pm is 100% PM10 by
engineering judgement
[(3.14 - 0.5) 66% + (0.5)100%]
= 72% < 10 urn. Assume 66% from
detergent spray dryer & 100%
from Ref. #288.
From AP-42, Table 8.1-2, assume
psd is same as uncontrolled
plant;14% < 10 urn.
Use Table 11.2.3-2 in AP-42; 36%
< 10 urn.
56
-------
Reference
Number
292a
292b
293.
294.
295.
SCC
296.
297.
298.
299.
300.
301.
302.
303.
304.
305.
3-05-002-04
3-05-002-11
3-05-003-01
3-05-003-03
3-05-003-08
3-05-003-11
3-05-004-02
3-05-004-03
3-05-005-05
3-05-006-07
PM Factor
0.1
1.7
70.0
34.0
20.0
0.02
3-05-003-12 0.6
3-05-003-14 0.065
3-05-003-15 0.88
3-05-003-16 18.8A
3-05-004-01 24.0
2.0
26.0
25.0
0.2
Basis For PM10 Derivative
Same as Ref. #291,
SCC 3-05-002-03
From AP-42 (10/86), Table
8.1-2; 21% < 10 urn.
oinrHar to ore.dr.jdng
< 10 urn
Assume psd similar to storage
piles. Ref. 291, SCC 3-05-002-
03; 36% < 10 urn
Assume psd for screening is
similar to Brick Raw Material
screening/grinding; AP-42, Table
8.3-4; 7% < 10 urn.
Use AP-42, Appendix C.2,
Category 5; 53% < 10 urn
Same as Ref. ?296.
Same as Ref. *296.
Same as Ref. ?296.
Same as Ref. #296.
Assume psd is similar to
electric arc melting in castable
refractories (SCC 3-05-005-03),
where 92% < 10 urn
Assume psd is similar to
raw material dryer in castable
refractories (SCC 3-05-005-01)
where 51% < 10 urn
Same as Ref. #301; 92% < 10 urn.
Assume molding similar to
materials handl ing, AP-42, App.
C.2, Cat. 8, 92% PM10: assume
shakeout similar to shakeout in
gray iron foundries, Table
7.10-5, 70% PM10. Avg. PM10 =
(92 + 70)/2 = 81% < 10 urn.
Assume psd similar to concrete
batching, cement unloading (SCC
3-05-011-07); 50% < 10 urn
57
-------
Referencs
Number
306.
307.
308.
309.
310.
311.
312.
313.
314.
315.
316.
317.
318.
319.
320.
321.
322.
323.
324.
sec
3-05-006-08
3-05-006-09
3-05-006-10
3-05-006-12
3-05-006-19
3-05-007-07
3-05-007-08
3-05-007-09
3-05-007-10
3-05-007-12
3-05-007-19
3-05-009-03
3-05-009-04
3-05-009-05
3-05-010-21
3-05-010-22
3-05-010-23
3-05-010-30
3-05-010-33
PM Factor
4.0
0.5
1.5
0.3
0.24
0.2
4.0
0.5
1.5
0.3
0.24
12.0
0.5
0.8
0.45
0.0001
0.1
0.05
1.3
Basis For PM1Q Derivative
Assume psd similar to storage
piles, Ref. 291, SCO 3-05-002-
03; 36% < 10 urn
Same as Ref. #302.
Assume psd for secondary
crushing produces a higher % of
fines than primary crushing,
assume 75% < 10 urn
From AP-42, Appendix C.2,
Category 3; 51% < 10 urn
From AP-42, Appendix C.2,
Category 4, 85% < 10 urn
Same as Ref. #305
Same as Ref. #306
Same as Ref. ?307
Same as Ref. =308
Same as Ref. =309
Same as Ref. =310
Use AP-42, App. C.2, Category
3; 51% < 10 urn
Assume psd similar to SCC
3-05-005-02; Use AP-42 Appendix
C.2, Category 3; 51% < 10 urn.
Same as Ref. #318.
No basis for technology
transfer. See AP-42, Section
8.24, Table 8.24-2.
See AP-42, Section 8.24 Table
8.24-2; Equation
Assume psd same as
3-05-006-07, Ref. #305,
unloading; 50% < 10 urn
Same as Ref. #320
Assume wet drilling similar to
stone drilling. From AP-42,
Table 8.19.2-2, 12.5% < 10 urn
58
-------
Reference
Number
325.
326.
327.
328.
329.
330.
331.
332.
333.
334.
335.
336.
337.
338.
339.
340.
341.
342.
sec
3-05-010-34
3-05-010-37
3-05-010-42
3-05-010-43
3-05-010-48
3-05-010-49
3-05-011-20
3-05-012-01
3-05-012-02
3-05-012-03
3-05-012-04
3-05-012-05
3-05-012-06
3-05-012-07
3-05-012-08
3-05-012-09
3-05-012-11
3-05-012-12
PM Facti
0.22
0.03
0.002
47,400
0.012
760.0
0.2
22.0
27.5
0.5
58.0
9.0
1.3
9.0
2.0
6.0
16.0
2.0
Basis For PM10 Derivative
Same as Ref. ?324
Assume psd same as Ref. #305,
SCC 3-05-006-07 - Raw Material
Unloading; 50% < 10 urn
Assume psd same as Ref. #305,
SCC 3-05-006-07; 50% < 10 urn
Assume same as Ref. #291,
SCC 3-05-002-03; 36% < 10 urn
Assume same as Ref. #305, SCC
3-05006-07; 50% < 10 urn
Assume same as Ref. #305, SCC
3-05-006-07; 50% < 10 urn
Assume psd similar to cement
unloading to storage bins (3-
05-011-07), bucket elevator; 50%
< 10 urn
Assume psd for furnaces similar
to melting furnace in glass mfg.
AP-42 Table 8.13-2; 95% < 10 urn
Same as Ref. #332,
SCC 3-05-012-01
Same as Ref. #332
SCC 3-05-012-01
No basis
transfer.
for technology
Assume PM is 100% < 10 urn;
engineering judgement.
Same as Ref. 336; 100% < 10 urn.
Same as Ref. #332; 95% < 10 urn.
No basis for technology
transfer.
Same as Ref. #336;
< 10 urn.
100%
Same as Ref. #332; 95% < 10 urn.
Same as Ref. ?332; 95% < 10 urn.
59
-------
Reference
Number
343.
344.
345.
346.
347.
348.
349.
350.
351.
352.
353.
354.
355.
sec
3-05-012-13
3-05-012-14
3-05-012-15
3-05-013-01
3-05-014-03
3-05-014-04
3-05-015-04
3-05-015-05
3-05-015-06
3-05-015-21
3-05-015-22
3-05-016-01
3-05-016-02
PM Factor
6.0
1.0
1.2
16.0
2.0
17.4
0.7
0.5
1.5
3.0
5.0
0.5
1.5
356.
357.
358.
359.
3-05-016-03
3-05-016-05
3-05-016-07
3-05-016-08
8.0
50.0
0.8
0.2
Basis For PM10 Derivative
Same as Ref. #332; 95% < 10 urn.
No basis for technology
transfer.
Same as Ref. =?336; 100%
< 10 urn.
Same as Ref. #332, 95% < 10 urn.
Same as Ref. #332, 95% < 10 urn.
Same as Ref. #332, 95% < 10 urn.
Assume psd same as conveying,
AP-42, (9/88), Table
8.19.2-2, 22% < 10 urn.
From AP-42, Appendix C.2,
Category 3, 51% < 10 urn
Assume psd similar to secondary
crushing of cement raw materials
(305-006-10); 75% < 10 urn
From AP-42, App. C.2,
Category 4, 85% < 10 urn
From AP-42, App. C.2,
Category 4; 85% < 10 urn
Same as Ref. #350,
SCO 3-05-015-05
Assume psd similar to secondary
crushing of gypsum ore
(3-05-015-06); 75% < 10 urn.
Assume psd similar to continuous
kettle calciner (3-05-015-11);
63% < 10 urn.
Assume psd similar to continuous
kettle calciner (3-05-015-11);
63% < 10 urn
Assume psd similar to conveying
(3-05-015-04); 22% < 10 urn
Assume psd similar to Raw
Material unloading, (3-05-012-
21); 50% < 10 urn
60
-------
Reference
Number
360.
361.
362.
363.
364.
365.
366.
367.
368.
369.
370.
371.
372.
373.
374.
375.
376.
377.
378.
sec
3-05-016-09
3-05-016-10
3-05-016-11
3-05-016-12
3-05-019-04
3-05-020-06
3-05-020-07
3-05-020-09
3-05-020-12
3-05-025-02
3-05-025-03
3-05-025-07
3-06-001-03
3-06-001-04
3-06-001-05
3-06-001-06
3-06-001-07
3-06-002-01
3-06-003-01
PM Factor
0.1
4.0
40.0
0.1
40.0
no factor*
0.33
0.16
35.0
0.33
0.029
3796.0
12. OS
3.0
3.0
3.0
0.27
242.0
17.0
Basis For PM1Q Derivative
Assume psd similar to spray
drying of detergents
(3-01-009-01); 67% < 10 urn
Assume similar to aggregate
piles in asphaltic concrete,
Ref. #291; 36% < 10 urn
Same as Ref. #356; 63% < 10 urn.
Same as Ref. #360; 67% < 10 urn.
Assume psd same as Raw Material
Storage Piles; 36% < 10 urn
Assume psd similar to storage
piles, SCC 3-05-016-10; 36%
< 10 urn
No basis for technology transfer
Assume psd is similar to
SCC 3-05-002-01; 14% < 10 urn
Same as Ref. #361; 36% < 10 urn.
Same as Ref. #358; 22% < 10 urn.
Same as Ref. #361; 36% < 10 urn.
Assume psd is similar to
residual oil fired in commercial
boilers; AP42, Table 1.3-5; 62%
< 10 urn
Same as Ref. #5
Same as Ref. #5
Same as Ref. #5
Same as Ref. #5
From API pub. 4363, FCCU with
internal cyclones emit PMwith
70% < 10 urn
Same as Ref. #377
*The PM factor of 2.0 Ib has been withdrawn.
61
-------
Reference
Number
379.
380.
SCC
381
382.
394.
395.
396.
3-06-012-01
3-07-001-08
3-07-001-10
3-07-004-02
3-07-008-04
3-07-008-05
3-07-008-06
PM Factor
523.0
72.0
230.0
0.6
383.
384.
285.
386.
387.
388.
389.
390.
391.
392.
393.
3-07-007-01
3-07-007-03
3-07-007-04
3-07-007-11
3-07-007-12
3-07-007-13
3-07-007-14
3-07-007-15
3-07-008-01
3-07-008-02
3-07-008-03
4.25
0.6
859.0
4.64
2.37
3.18
4.14
3.7
0.02
0.35
1.0
2.25
2.25
4.0
Basis For PM1Q Derivative
Same as Ref. #377
All fluid bed calciners
are well controlled for
product collection. PM is
likely to be fine; assume
psd similar to fluid coking
(3-06-01201); 70% < 10 urn
Assume psd similar to recovery
boiler w/o direct contact
evaporator, Table 10.1-3,
AP-42; 100% < 10 urn
No basis for technology
transfer. As default value,
assume psd is similar to cotton
ginning; avg. psd; 58% < 10 urn
Same as Ref. #382
Same as Ref. #382
Same as Ref. =382
Same as Ref. =382
Same as Ref. =382
Same as Ref. #382
Same as Ref. #382
Same as Ref. #382
Same as Ref. #382
Same as Ref. #382
Assume psd is similar to
storage piles, Ref. #291,
SCC 3-05-002-03; 36% < 10 um
PSD from test data reported by
CA Air Resources Board; 40%
< 10 um.
Same as Ref. #394; 40% < 10 um.
Assume psd from sanding to
consist of higher % of fines
than from sawing. Assume 50%
< 10 um.
62
-------
Reference
Number SCC PM Factor Basis For PM10 Derivative
397. 3-07-008-07 5.0 Same as Ref. #396; 50% < 10 urn.
398. 3-07-008-08 2.0 Same as Ref. #394; 40%<10um.
399. 3-07-030-01 1.0 Same as Ref. #382; 58% < 10 urn.
400. 3-07-030-02 2.0 Same as Ref. #382; 58% < 10 urn.
401. 3-09-025-01 0.035 Assume psd is similar to
3-04-002-32, Ref. #240, wire
incinerator fugitive emissions;
60% < 10 urn
402. 3-10-004-01 2.0 Assume psd is similar to
external combustion boiler
firing distillate oil; AP-42,
Table 1.3-4; 50% < 10 urn
403. 3-10-004-02 12.OS Same as above for residual oil:
AP-42, Table 1.3-3; 86% < 10 urn
404. 3-10-004-03 12.OS Assume psd for crude oil is
similar to residual oil (3-10-
004-02); 86% < 10 urn
405. 3-10-004-04 3.0 Assume psd is similar to
1-02-006-01 100% < 10 urn
406. 3-10-004-05 3.0 Assume psd is similar to SCC
1-02-006-01; 100% < 10 urn
407. 3-10-004-11 2.0 Assume psd is similar to
oil fired industrial external
combustion boiler
(1-02-005-01); 50% < 10 urn
408. 3-10-004-12 12.OS Assume psd is similar to
residual oil fired external
comb, boilers (102-004-01); 86%
< 10 urn
409. 3-10-004-13 12.OS Assume psd is similar to
residual oil fired external
combustion boilers
(1-02-004-01); 86% < 10 urn
410. 3-10-004-14 3.0 Same as Ref. #5
411. 3-10-004-15 3.0 Assume psd is similar to process
gas fired boiler
(1-02-007-01); 100% < 10 urn
63
-------
Reference
Number SCC PM Factor
412. 3-60-001-01 0.7
413.
414.
415.
416.
417.
418.
419.
420.
421.
422.
423.
4-02-016-01
5-01-005-05
5-01-005-07
5-01-005-08
5-01-005-10
5-01-005-11
5-01-005-12
5-02-001-01
5-02-001-02
5-02-001-03
5-02-001-04
9.68
8.0
20.0
7.0
13.0
138.0
37.0
7.0
15.0
1.4
20.0
Basis For PM10 Derivative
Assume psd similar to secondary
lead smelting in pot furnace
(3-04-00401); 25% < 10 urn
Assume psd similar to detergent
spray drying (3-01-009-01);
66.1% < 10 urn
Assume psd similar to municipal
waste "starved air" incinerator:
AP-42, (9/88), Table 2.1-2 ; 74%
< 10 urn
Assume psd similar to refuse
derived fuel in municipal waste
combustion: AP-42, TAble 2.1-
2; 55% < 10 urn
Assume psd similar to refuse
derived fuel in municipal waste
combustion: AP-42, Table
2.1-2; 55% < 10 urn
Assume psd similar to municipal
waste mass burn incinerator; AP-
42, App. C.I, Table 2.1; 38%
< 10 urn
Assume psd similar to municipal
waste mass burn incinerator;
App. C.I, Table 2.1; 38%
< 10 urn
Assume psd similar to municipal
waste mass burn incinerator;
App. C.I, Table 2.1; 38%
< 10 urn
Assume psd is similar to
municipal waste modular
incinerator; AP-42, App. C.I,
Table 2.1; 67% < 10 urn
Assume psd is similar to
municipal waste mass burn
incinerator, AP-42, App. C.I,
Table 2.1; 38% < 10 urn
Assume psd is similar to
AP-42, Table 2.1-2; 74%
< 10 urn
Assume same as Ref. #
64
-------
Reference
Number SCC
424.
425.
426.
427.
428.
429.
430.
431.
432.
433.
434.
435.
436.
437.
5-02-001-05
5-02-003-01
5-02-003-02
5-02-005-05
5-03-001-01
5-03-001-02
5-03-001-03
5-03-001-04
5-03-001-05
5-03-001-06
5-03-001-07
5-03-001-08
5-03-001-09
5-03-002-04
PM Factor
7.0
30.0
6.0
8.0
7.0
15.0
1.4
20.0
7.0
13.0
138.0
2.0
37.0
0.9
Basis For PM10 Derivative
Assume same as Ref. #416
Assume same as Ref.
Assume same as Ref.
Assume same as Ref.
Assume same as Ref.
Assume same as Ref.
Assume same as Ref.
Assume same as Ref.
Assume same as Ref.
Assume same as Ref.
Assume same as Ref.
#418
#420
#414
#420
#421
#422
#415
#416
#417
#418
Assume psd is similar to
3-04-00232, wire incinerator
fugitive emissions; 60%
< 10 urn
Assume same as Ref.
No basis for technol
#419
ogy
transfer. As default value,
assume
L t0°J
On. obserued
< 10 urn,
65
-------
TECHNICAL REPORT DATA
iPlcasc read Instructions on ihe reverse before completing/
REPORT NO.
EPA-450/4-89-022
2.
3. RECIPIENT'S ACCESSION NO.
TITLE AND SUBTITLE
PM,Q Emission Factor Listing Devrloped By Technology
Transfer and AIRS Source Classification Codes Wtih
Documentation
5. REPORT DATE
November 1989
. PERFORMING ORGANIZATION CODE
AUTHOR(S)
8. PERFORMING ORGANIZATION REPORT NO.
PERFORMING ORGANIZATION NAME AND ADDRESS
U.S. Environmental Protection Agency
Office of Air and Radiation
Office of Air Quality Planning and Standards
Research Triangle Park, NC 27711
10. PROGRAM ELEMENT NO.
11. CONTRACT/GRANT NO.
2. SPONSORING AGENCY NAME AND ADDRESS
13. TYPE OF REPORT AND PERIOD COVERED
14. SPONSORING AGENCY CODE
S. SUPPLEMENTARY NOTES
). ^\jrr ucnncil 1 *4 n T r*\J I CO
The listing supplements AP-42, Compilation of Air Pollutant Emission Factors,
Fourth Edition.
6. ABSTRACT
This report provides a listing of particulate matter emission factors,
size-specific £10 micrometers (PM,Q) for fuel combustion, inductrial and
commercial operations, and solid wastes disposals. The factor list is identified
with appropriate EPA AIRS Facility Subsystem (AFS) Source Classification Codes
(SCCs) and their process descriptions. An appendix to the listing provides
documentation of technology transfer rationale for the PM,Q emission factors.
KEY WORDS AND DOCUMENT ANALYSIS
DESCRIPTORS
3.IDENTIFIERS/OPEN ENDED TERMS
c. COSATI Field/Group
Emission Factors
Particle Size Emission Factors
PM,g Emission Factors
ComHustion Sources
Industrial Processes
Solid Wastes Combustion
Air Emissions
18. DISTRIBUTION STATEMENT
19. SECURITY CLASS (This Report)
21. NO. OF PAGES
63
20. SECURITY CLASS (Tliis pagel
22. PRICE
EPA Form 2220-1 (R«». 4-77) PREVIOUS EDITION is OBSOLETE
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