# Enclosure 1

### ENCLOSURE 1 

# INFORMATION COLLECTION REQUEST FOR Off -Site Waste and Recovery Operations This information collection request is being conducted by the Environmental Protection Agency’s (EPA) Office of Air and Radiation (OAR) to assist the EPA Administrator in developing emission standards for Off

-Site Waste and Recovery Operations under Clean Air Act (CAA) section 112. The survey is being sent under the authority of Section 114 of the CAA. BACKGROUND: Section 112 (d) of the Clean Air Act (CAA) calls for EPA to promulgate national technology

-based emission standards for hazardous air pollutants (NESHAP) for sources emitting one or more of the HAP listed in CAA section 112(b). For major sources, these technology

-based standards must reflect the maximum degree of emissions reductions of HAP achievable (after considering cost, energy requirements, and nonair quality health and environmental impacts). In addition, under CAA section 112(d)(6), EPA is required to review the technology

-based standards and revise them “as necessary (taking into account developments in practices, processes, and control technologies)” no less frequently than every 8 years. Furthermore, we are required by section 112(f) (2) of the Clean Air Act (CAA) to assess the risk remaining (residual risk) eight years after the promulgation of maximum achievable control technology (MACT) standards under section 112(d). If we find the residual risk fails to protect public health with an ample margin of safety or to prevent (taking into consideration various factors) adverse environmental effects, we are required to promulgate more stringent standards. The Off

-Site Waste and Recovery Operations maximum achievable control technology (MACT) standards were promulgated on July 1, 1996 (see 61 FR 34140). We are collecting specific detailed information to support development of standards as part of our review as described above. Please note this survey is for off

site waste and recovery operations only. CAA section 114(a) states that the Administrator may require any person who owns or operates any emission source, who manufactures emission control equipment or process equipment, who the Administrator believes may have information necessary for the purposes set forth in section 114(a), or who is subject to any requirement of the CAA (other than certain provisions under Title II), to provide EPA with information for the following purposes: 1. Developing or assisting in the development of the following: a. State implementation plans (§§ 110 and 111(d)); b. New Source Performance Standards (NSPS) (§ 111); c. National Emissions Standards for Hazardous Air Pollutants (NESHAP) (§ 112); d. Solid waste combustion or other related solid waste regulations (§ 129); 2. Determining whether any person is in violation of any standards or requirements developed under the authorities cited above; or 3. Carrying out any provision under the CAA (except certain provisions under Title II). The Administrator may require that those persons identified above do the following so the Administrator may have the information necessary for the items listed in #1

-3:

 establish and maintain records;
 make reports;

###  install, use, and maintain monitoring equipment, and use audit procedures, or methods;
 sample emissions (in accordance with such procedures or methods, at such locations, at such intervals, during such periods, and in such manner as the Administrator shall prescribe);
 keep records on control equipment parameters, production variables or other indirect data when direct monitoring of emissions is impractical;
 submit compliance certifications in accordance with section 114(a)(3); and
 provide such other information as the Administrator may reasonably require. DIRECTIONS:

 All recipients must complete and return this survey by April 10, 2013

.

 Please identify clearly any response(s) that you consider to be confidential business information (CBI). Any responses not so identified will be included in a publicly available database. Refer to Enclosures 3, 4, 5, and 6 for more information on the treatment of CBI and a list of information you may be asked to submit later to substantiate a claim of confidentiality. DEFINITIONS: For the purposes of this ICR only, terms used have the meanings attributed to them in 40 CFR 63.681. CONFIDENTIAL BUSINESS INFORMATION (CBI) : Please indicate if any CBI is included in this survey response: 

##  Y 

##  N OFF - SITE WASTE AND RECOVERY OPERATIONS We believe that you own a facility that has Off

-Site Waste and Recovery Operations . If you believe that this survey does not pertain to you, please indicate your reason below: 

##  The Off

-Site Waste and Recovery Operations are permanently shut down. Please also identify the date the Off

-Site Waste and Recovery Operations were shut down, what steps were taken to close the equipment or stop operations , and if you still have a permit

.

_________________________________________________________________________________

________________________________________________________________________________

________________________________________________________________________________ 

##  No Off

-Site Waste and Recovery Operations at this facility. Please identify the operations at the facility.

________________________________________________________________________________

________________________________________________________________________________

________________________________________________________________________________ If your facility does not have Off -Site Waste and Recovery Operations, please respond as soon as possible. We will review that information and respond as to whether you need to complete any other part of the survey.

# Enclosure 2

### U.S. EPA Information Collection Request for Off-Site Waste and Recovery Operations

P age 1 of 13 General Information Name of Legal Owner: Clean Harbors Aragonite, LLC Legal Owner Address: 11600 North Aptus Road, Aragonte, UT 84029 Number of Legal Owner Employees: Same Facility Name: Clean Harbors Aragonite, LLC Facility Address: 11600 North Aptus Road, Aragonte, UT 84029 Mailing Address (if different from facility address): Facility Contact Name: Scott Kuhn Facility Contact Title: VP Environmental Compliance Facility Contact Phone Number: 803-691-3426 Facility Contact Email Address: 400 Arbor Lake Drive, Suite 900-B Number of Company Employees at the Entire Facility: 128 Please enter any other comments regarding general ownership information here: None

### U.S. EPA Information Collection Request for Off-Site Waste and Recovery Operations

Page 2 of 13 Facility Information Is the facility a major source for HAP? (see definition below) Major sources are any stationary source or group of stationary sources located within a contiguous area and under common control that emits or has the potential to emit considering controls, in the aggregate, 10 tons per year (TPY) or more of any hazardous air pollutant or 25 TPY or more of any combination of HAP. Are there one or more off-site waste management or recovery operations at the facility subject to the Off-Site Waste and Recovery Operations (OSWRO) MACT (40 CFR 63, subpart DD)? Is the facility exempt from complying with the OSWRO MACT?

What type(s) of off-site waste does the facility accept? (please include shipment method, physical form (i.e., solid, liquid, sludge), and a general description) Approximately how many sources (facilities) does that waste come from? What is the base year for which information is being provided? (please limit reporting years between 2006 and 2012, and provide the most current year) For this base year, what was the amount of off-site waste received? (please specify units; e.g., gal/yr) For this base year, what was the HAP content of the off-site waste received? (please specify units; e.g., tons) How many hours per year are control devices bypassed to the atmosphere to perform routine maintenance? Are any OSWRO operations scheduled to be discontinued?

Are any OSWRO operations scheduled to be added or expanded?

What is the permitting classification of your facility?
What are the operating permit IDs for the OSWRO operations at your facility? Is your operating permit available online?

Please provide the coordinates (in decimal degrees) of your facility property boundary at each corner (node). Alternatively, please provide the minimum distance from any OSWRO emission point to the facility property boundary.
Please enter any other comments regarding the facility here: If yes, please provide date(s) that addition(s) and/or expansion(s) will begin production and explain changes: If yes, please provide dates of closure and explain changes: 2011
58,000 tons/yr

Varies If yes, please explain:

None

40d44m14.31sN, 112d59m16.78sW; 40d43m57.10sN, 112d59m17.18sW; 40d43m57.10sN, 112d59m01.32sW, 40d43m14.31sN, 112d59m01.32sW Facility accepts all EPA waste codes except for the following; radioactive waste,Explosive material, as defined by the Department of Transportation under 49 CFR Part 173;Dioxin-containing wastes, identified by EPA as F020, F021, F022, F023, F026, and F027 wastes in 40 CFR 261.31.

Over 3000

Permit Number 4500048002

If yes, please provide a link to or a copy of your most recent operating permit. If no, please provide a copy of your most recent operating permit.

### U.S. EPA Information Collection Request for Off-Site Waste and Recovery Operations

Page 3 of 13 If no, please explain.

If no, please explain.

If "Other", please explain:

If "Other", please explain: 

### AP-42 Emission factors are used to estimate emissions

If neither apply, please explain:

If yes, please describe the control technique(s): 

### Please provide the additional capital and annual costs of this practice above that required by the OSWRO NESHAP:

Pumps 29 Compressors 0 Agitators 16 Pressure relief devices 16 Sampling connection systems 16 Open-ended valves or lines 910 Valves; 0 open-ended lines; 0 open-ended valves Connectors 1350 Instrumentation systems 2 Facility is subject to RCRA Subpart BB and CC requirements and CAA Subpart DD requirements. Please enter any other comments regarding equipment leaks here: What is the number of each type of component for the equipment in OSWRO HAP service (equipment that contacts off-site material having a total HAP concentration ≥ 10% by weight for 300 hours/year or more)? With which subpart do you comply for equipment leaks? Please provide documentation demonstrating the basis for the equipment leak emissions estimates. What type of documentation are you providing? Equipment Leaks Have you verified and/or corrected the equipment leak emissions for your OSWRO processes in Enclosure 2A?

Have you completed all control information fields for your OSWRO equipment leaks in Enclosure 2A?

What emissions calculation approach was used to estimate the equipment leak emissions?

Are you implementing work practices or other HAP control techniques beyond those required by the MACT standard?

### U.S. EPA Information Collection Request for Off-Site Waste and Recovery Operations

If no, please explain. 

### Information on transfer systems included in GRP emission ID

If no, please explain.

If "Other", please explain:

If "Other", please explain: 

### AP-42 Emission factors used to estimate emissions

If yes, please describe the control technique(s): 

### Please provide the additional capital and annual costs of this practice above that required by the OSWRO NESHAP:

Please enter any other comments regarding transfer systems here: Transfer Systems Have you entered the OSWRO transfer system emissions in Enclosure 2A?

Have you completed all control information fields for your OSWRO transfer systems in Enclosure 2A?

What emissions calculation approach was used to estimate the transfer system emissions?

Are you implementing work practices or other HAP control techniques beyond those required by the MACT standard? Please provide documentation demonstrating the basis for the transfer system emissions estimates.Are you providing emissions factors or source test data?

### U.S. EPA Information Collection Request for Off-Site Waste and Recovery Operations

If no, please explain. 

### No oil-water or organic-water separators

If no, please explain. 

### No oil-water separators

If "Other", please explain:

If "Other", please explain:

If yes, please describe the control technique(s): 

### Please provide the additional capital and annual costs of this practice above that required by the OSWRO NESHAP:

No oil-water separators at the facility.Please enter any other comments regarding organic or oilwater separators here: Are you implementing work practices or other HAP control techniques beyond those required by the MACT standard? Please provide documentation demonstrating the basis for the oil-water and organic-water separators emissions estimates.Are you providing emissions factors or source test data? Oil-water and organic-water separators Have you entered the OSWRO oil-water and organic-water separators emissions in Enclosure 2A?

Have you completed all control information fields for your OSWRO oil-water and organic-water separators in Enclosure 2A?

What emissions calculation approach was used to estimate the oil-water and organic-water separators emissions?

### U.S. EPA Information Collection Request for Off-Site Waste and Recovery Operations

If no, please explain.

If no, please explain.

If "Other", please explain:



### Please list eachOSWRO container requiring Level 1 or Level 2 control:
Container ID Container capacity Container emissions control level implemented No container numbers are assigned >26 gallon; <119 gallon Level 1 No container numbers are assigned >119 gallon Level 2 

### Please provide the additional capital and annual costs of this practice above that required by the OSWRO NESHAP: 40 CFR 63.922 and 63.923 If "Other", please explain:



### Please enter any other comments regarding containers here: The facility is subject to Level 1 and Level 2 control requirements under RCRA and Level 1 and Level 2 controls under Subpart DD of Part 63 (add information for more containers as necessary) Containers Have you entered the OSWRO containers emissions in Enclosure 2A?

Have you completed all control information fields for your OSWRO containers in Enclosure 2A?

What emissions calculation approach was used to estimate the containers emissions?

Are you implementing work practices or other HAP control techniques beyond those required by the MACT standard? Please provide documentation demonstrating the basis for the containers emissions estimates. Are you providing emissions factors or source test data? Facility permit contains no numeric emission limits

Technical approach prescribed in regulations; Level 1 and Level 2 control requirements

If yes, please describe the control technique(s):

### U.S. EPA Information Collection Request for Off-Site Waste and Recovery Operations

If no, please explain. 

### No surface impoundments at the facility

If no, please explain.

If "Other", please explain:

If "Other", please explain:



### No surface impoundments at the facility Please enter any other comments regarding surface impoundments here: If yes, please describe the control technique(s): 

### Please provide the additional capital and annual costs of this practice above that required by the OSWRO NESHAP: Surface Impoundments Have you entered the OSWRO surface impoundments emissions in Enclosure 2A?

Have you completed all control information fields for your OSWRO surface impoundments in Enclosure 2A?

What emissions calculation approach was used to estimate the surface impoundments emissions?

Are you implementing work practices or other HAP control techniques beyond those required by the MACT standard? Please provide documentation demonstrating the basis for the surface impoundments emissions estimates.Are you providing emissions factors or source test data?

### U.S. EPA Information Collection Request for Off-Site Waste and Recovery Operations

Page 8 of 13 If no, please explain.

If no, please explain.

There are no process vents at the facility. 

### Please enter any other comments regarding process vents here: If "Other", please explain:

If yes, please describe the control technique(s): 

### Please provide the additional capital and annual costs of this practice above that required by the OSWRO NESHAP: Please provide documentation demonstrating the basis for the process vent emissions estimates. Are you providing emissions factors or source test data?

Are you implementing work practices or other HAP control techniques beyond those required by the MACT standard? If "Other", please explain: Process Vent Emissions Information Have you verified and/or corrected the process vent emissions for your OSWRO processes in Enclosure 2A?

Have you completed all control information fields for your OSWRO process vent streams in Enclosure 2A?

What emissions calculation approach was used to estimate the process vent emissions? No process vents at the facility

No process vents at the facilty

### U.S. EPA Information Collection Request for Off-Site Waste and Recovery Operations

Page 9 of 13 Tanks Emissions Information

Please list eachOSWRO tank requiring Level 1 or Level 2 control:

Tank ID Tank capacity Tank content MTVP 1 

### Tank content AVP 2 

### Tank height Tank diameter Tank average annual throughput Tank emissions control equipment
T-301 29,395 gal 9.78 4.41 26' 7" 15' 1" Incinerator w/backup carbon
T-302 29,395 gal 9.78 4.41 26' 7" 15' 1" Incinerator w/backup carbon
T-303 29,395 gal 9.78 4.41 26' 7" 15' 1" Incinerator w/backup carbon
T-304 29,395 gal 9.78 4.41 26' 7" 15' 1" Incinerator w/backup carbon
T-305 29,395 gal 9.78 4.41 26' 7" 15' 1" Incinerator w/backup carbon
T-306 29,395 gal 9.78 4.41 26' 7" 15' 1" Incinerator w/backup carbon
T-307 29,395 gal 9.78 4.41 26' 7" 15' 1" Incinerator w/backup carbon
T-308 29,395 gal 9.78 4.41 26' 7" 15' 1" Incinerator w/backup carbon
T-309 29,395 gal 9.78 4.41 26' 7" 15' 1" Incinerator w/backup carbon
T-310 29,395 gal 9.78 4.41 26' 7" 15' 1" Incinerator w/backup carbon
T-311 29,395 gal 9.78 4.41 26' 7" 15' 1" Incinerator w/backup carbon
T-312 29,395 gal 9.78 4.41 26' 7" 15' 1" Incinerator w/backup carbon
T-321 29,395 gal 9.78 4.41 26' 7" 15' 1" Incinerator w/backup carbon
T-322 29,395 gal 9.78 4.41 26' 7" 15' 1" Incinerator w/backup carbon
T-323 29,395 gal 9.78 4.41 26' 7" 15' 1" Incinerator w/backup carbon
T-324 29,395 gal 9.78 4.41 26' 7" 15' 1" Incinerator w/backup carbon
T-401 33,538 gal 6.01 4.41 24' 14' x 35' Incinerator w/backup carbon
T-406 5780 gal 6.01 4.41 12' x 14'3" 10'1" Incinerator w/backup carbon

T-403 120 Cubic yards 4.41 0.67 18' 6" 17'5" x 17'6" T-enclosure with Incinerator w/backup carbon

T-404B-East

T-404B-West

T-404A 500 cubic yards 4.41 0.67 17'11" X 37'9" 18'6" T-enclosure with Incinerator w/backup carbon
1

### Maximum True HAP Vapor Pressure 2

### Average HAP Vapor Pressure For each tank with an internal floating roof, please list the slotted ladder information:

Tank ID Number of ladders with slotted legs Gasketed deck cover over slotted ladder(s)? Ladder sleeve over slotted ladder(s)? Pole wipers in place for slotted ladder legs? None



### For each tank with a fixed roof, please list the tank fitting information: If yes, please describe the control technique(s): 

### Please provide documentation demonstrating the basis for the tanks emissions estimates.Are you providing emissions factors, source test data or other data?

Are you implementing work practices or other HAP control techniques beyond those required by the MACT standard? If "Other", please explain:

If "Other", please explain:



### (add information for more tanks as necessary)

(add information for more tanks as necessary) Please provide the additional capital and annual costs of this practice above that required by the OSWRO NESHAP: Have you entered the tanks emissions for your OSWRO processes in Enclosure 2A?

Have you completed all control information fields for your OSWRO storage vessels in Enclosure 2A?

What emissions calculation approach was used to estimate the tank emissions? If no, please explain.

If no, please explain.

T-enclosure with Incinerator w/backup carbon Approximately 5.0 MM gallons of waste

through all of the liquid tanks per year.

Approximately 32,000 cubic yards of solid waste through these tanks per year. 500 cubic yards 18'6" 17'11" X 37'9" 4.41 0.67

### U.S. EPA Information Collection Request for Off-Site Waste and Recovery Operations

Page 10 of 13 Tanks Emissions Information

Tank ID Number of access hatches Number of gauge hatches Number of conservation vents Number of valves/instruments Number of emergency pressure relief vents T-301 

### 2 1 0 14 1 T-302 

### 2 1 0 14 1 T-303 

### 2 1 0 14 1 T-304 

### 2 1 0 14 1 T-305 

### 2 1 0 14 1 T-306 

### 2 1 0 14 1 T-307 

### 2 1 0 14 1 T-308 

### 2 1 0 14 1 T-309 

### 2 1 0 14 1 T-310 

### 2 1 0 14 1 T-311 

### 2 1 0 14 1 T-312 

### 2 1 0 14 1 T-321 

### 2 1 0 14 1 T-322 

### 2 1 0 14 1 T-323 

### 2 1 0 14 1 T-324 

### 2 1 0 14 1 T-401 

### 2 3 0 10 0 T-406 

### 0 0 0 3 0

1

### Maximum True HAP Vapor Pressure For each tank with a floating roof (internal or external), please list the tank information:

Tank ID Annual number of days roof rests on landing legs Length of landing legs None



### Please enter any other comments regarding tanks here: No floating roof tanks used 

### (add information for more tanks as necessary)

(add information for more tanks as necessary)

### U.S. EPA Information Collection Request for Off-Site Waste and Recovery Operations

Page 11 of 13 Off-Site Material Treatment

If you treat off-site waste using biological degradation, please answer the following questions: What method of off-site waste HAP reduction is used?

How do you characterize the components of the waste products you receive that are treated with biological degradation? NA



### Please enter any other comments regarding off-site waste treatment here: NA 

### Do you perform any testing or other practices to determine whether fouling agents may be in the waste received? NA If "Other" or more than one of the above applies, please explain.

### U.S. EPA Information Collection Request for Off-Site Waste and Recovery Operations

Page 12 of 13 Startup and Shutdown Events

If no for any of the above, please explain: The operating units run continuously and emissions are vented to the facility hazardous waste incinerator. When the incinerator shuts down, emissions are directed to a backup carbon absorption system. As such there is no startup and shutdown of the emission source. Equipment Leaks Transfer Systems Organic and Oil-Water Separators Containers

Surface Impoundments
Process Vents Organic and Oil-Water Separators

Tanks Process Vents T he United States Court of Appeals for the District of Columbia Circuit vacated portions of two provisions in the EPA’s CAA section 112 regulations governing the emissions of HAP during periods of startup, shutdown and malfunction (SSM). Sierra Club v. EPA, 551 F.3d 1019 (D.C. Cir. 2008). Specifically, the Court vacated the SSM exemption contained in 40 CFR 63.6(f)(1) and 40 CFR 63.6(h)(1), that are part of a regulation, commonly referred to as the “General Provisions Rule,” that the EPA promulgated under section 112 of the CAA. When incorporated into CAA section 112(d) regulations for specific source categories, these two, now vacated, provisions exempted sources from the requirement to comply with the otherwise applicable CAA section 112(d) emission standard during periods of SSM. To be consistent with the Court’s decision, facilities must comply with the applicable standards at all time s.
For each emission source type, do the annual emissions estimate in the Enclosure 2A "Emissions (TPY)" field include the annual emissions from startup and shutdown events that you added in the "STARTUP EMISSIONS (TPY)" and "SHUTDOWN EMISSIONS (TPY)" fields? Please enter a separate response for each emissions point type below:

For each emission source type, can you comply with the emissions limitation and/or work practices in the regulation that apply during normal operation during startup and shutdown events? Please enter a separate response for each emissions point type below: Surface Impoundments

Tanks

Equipment Leaks Transfer Systems

Containers

### U.S. EPA Information Collection Request for Off-Site Waste and Recovery Operations

Page 13 of 13 Startup and Shutdown Events Please provide the following information about all startup and shutdown events:

None

Yes

NA

NA They are not directed to atmosphere. They are directed to backup carbon system.

Never

NA

NA

NA

NA Carbon absorption is used as a backup device so no startup or shutdown actually occurs

NA

NA



### Please enter any other comments regarding startup or shutdown here: None 

### 6. How do you determine the HAP emissions during the event? 7. How are control devices and work practices used to minmize emissions during the startup or shutdown event? 8. What compliance determination method(s) do you use during startup and shutdown events (e.g., monitor with CEMS)?

9.a. Please describe how HAP emissions would be minimized.
9 .b. How much would it cost to minimize HAP emissions in this manner? 9.c. How much would HAP emissions be reduced compared to an uncontrolled event? (If "emission factor" is used as basis for emissions estimate, please provide the emission factor and sources of the emission factor. 1 

### ) 4. What marks the end of the startup or shutdown event?

9. During startup and shutdown events, if you cannot comply with the emissions limitation and/or work practices in the regulation that apply during normal operation, what is the minimum emissions level that could be achieved?

1If "source test" is used as basis for emissions estimate, please provide a copy of the source test. 

### 5. What safety issues are connected with a startup or shutdown event? 1. What emissions source types experience startup and shutdown events?

2. How often do startup or shutdown events occur? 3. What is the average and range of event duration? 1.d. How are emissions released to the atmosphere (e.g., through a pressure relief device)? 1.c. How does the startup or shutdown event compare to normal operations (e.g., differences in flowrate, temp., pressure, alternate fuels used, alternate control devices used, etc.)? 1.a. Under normal operating conditions, do these emissions sources operate continuously? 1.b. What triggers the equipment to experience a startup or shutdown event (e.g. hot startup, startup after an emergency shutdown, re-start, control device startup)?

# Enclosure 2aEnclosure 2a

Page 1 p this table for all

Facility Name Emission Unit ID Proces s ID Emissio n Release Point ID SCC Code 1 Emissions Start Date Emissions End Date Pollutant CAS Number2 Pollutant Name (include organic and non-organic pollutants) Actual Emissio ns (TPY) MACTAllowable Emissions

(TPY) 3 Routine Emission

s Max Hourly (lbs/hr) Startup Emissio ns (TPY) Startup Emissio ns (lbs/hr) Shutdo wn Emissio ns (TPY) Shutdo wn Emissio ns (lbs/hr) MACT Source Category Emission Release Point Type4 Stack Height (ft) Exit Gas Temperatu re (° F) Stack Diameter (ft) Exit Gas Velocity (ft/sec) Exit Gas Flow Rate (ft3/sec) FugitiveLength (EW) (ft) FugitiveWidth (NS) (ft) Fugitive Angle (degrees) 5 Longitude (decimal degrees) 6 Latitude (decimal degrees) 6 Is Control Measur

e In Place? Control Measure 7 Control Measur e Efficien cy Comments EXAMPLE ENTRY: American Welding Paducah Plant 25 25 25 50310001 01/01/10 12/31/10 100414 Ethyl Benzene 2.45 4.32 6.7 1.24 0.08 0.61 0.2 Off-Site Waste and Recovery Operations vertical 44 1600 3.099999905 3.86999989 1758 NA NA NA -72.0789032 41.44273758 yes flare 98% reduction efficency based on manufacturer guarantees Clean Harbors Aragonite, LLC TNK1 TNK1 TNK1 50310003 1/1/2011 12/31/2011 NA VOC's 0.164 No limit specified in permit 0.037 NA NA NA NA Tanks fugitive varies ambient NA NA NA NA NA NA -112.985849 40.73498 yes Combustor 99.99 Incinerator Clean Harbors Aragonite, LLC TNK2 TNK2 TNK2 50310003 1/1/2011 12/31/2011 NA VOC's 0.011 No limit specified in permit 0.0025 NA NA NA NA Tanks fugitive varies ambient NA NA NA NA NA NA -112.985849 40.73498 yes Combustor 99.99 Incinerator
Clean Harbors Aragonite, LLC TNK3 TNK3 TNK3 50310003 1/1/2011 12/31/2011 NA VOC's 4.03E-07 No limit specified in permit 1.00E-08 NA NA NA NA Tanks fugitive varies ambient NA NA NA NA NA NA -112.985849 40.73498 yes Cover vented to control device 99.99 T-Enclosure followed by incinerator

Clean Harbors Aragonite, LLC GRP GRP GRP 50310001 1/1/2011 12/31/2011 NA VOC's 2.96 No limit specified in permit 0.675 NA NA NA NA Equipment leaks, transfer systems, fugitive varies ambient NA NA NA NA NA NA -112.985849 40.73498 no Leak detection and repair program Clean Harbors Aragonite, LLC CNT CNT CNT 50310002 1/1/2011 12/31/2011 NA VOC's NA No limit specified in permit NA NA NA NA NA Containers fugitive varies ambient NA NA NA NA NA NA -112.985849 40.73498 yes Pollution prevention technique Level 1 and Level 2 Container Controls

1 For SCC Code, please input one of the following codes: SCC SCC Description 50310001 Waste Disposal, Solid Waste Disposal-Industrial, Non-TSDF Treatment, Storage, Disposal Processes, Equipment Leaks 50310002 Waste Disposal, Solid Waste Disposal-Industrial, Non-TSDF Treatment, Storage, Disposal Processes, Containers 50310003 Waste Disposal, Solid Waste Disposal-Industrial, Non-TSDF Treatment, Storage, Disposal Processes, Tanks 50310004 Waste Disposal, Solid Waste Disposal-Industrial, Non-TSDF Treatment, Storage, Disposal Processes, Organic and Oil-Water Separators 50310005 Waste Disposal, Solid Waste Disposal-Industrial, Non-TSDF Treatment, Storage, Disposal Processes, Surface Impoundments 50310006 Waste Disposal, Solid Waste Disposal-Industrial, Non-TSDF Treatment, Storage, Disposal Processes, Transfer Systems 50310007 Waste Disposal, Solid Waste Disposal-Industrial, Non-TSDF Treatment, Storage, Disposal Processes, Process Vents

2See List of HAPs

3MACT- allowable

4Emission point

5Fugitive Angle: Specifies the rotation of the source from north (in the clockwise direction). The location coordinates should reflect the southwest corner of the area source as shown in this graphic:

6 Location of stack or southwest corner of a fugitive emissions release point

7For control measures, please include all control measures used for that emission point, including but not limited to:

Activated Carbon Adsorption list specific type in Control Measure Comments column

Combustor list specific type in Control Measure Comments column Electrostatic Precipitator Fabric Filter/Baghouse Flare Pressurized Tank Fixed Roof Tank (annual average if the parameter varies) Vertical Emissions Release Point Parameters Fugitive Emissions Release Point ParametersEnclosure 2a

Page 2 Fixed Roof Tank Vented to Control Device External Floating Roof Tank Fixed Roof Tank with Internal Floating Roof Vapor Balancing Floating Membrane Cover Cover Vented to Control Device High-Efficiency Particulate Air Filter (HEPA) Leak Detection and Repair Program Condenser

Scrubber list specific type in Control Measure Comments column
Multiple Controls in Series list specific types in Control Measure Comments column
Other Control Device describe in Control Measure Comments column
Pollution Prevention Technique describe in Control Measure Comments column
Process Modification describe in Control Measure Comments column

# DRAFT
Pollutant Name CAS No. Acetaldehyde 75070 Acetamide 60355 Acetonitrile 75058 Acetophenone 98862 2-Acetylaminofluorene 53963 Acrolein 107028 Acrylamide 79061 Acrylic acid 79107 Acrylonitrile 107131 Allyl chloride 107051 4-Aminobiphenyl 92671 Aniline 62533 o-Anisidine 90040 Asbestos 1332214 Benzene (including benzene from gasoline) 71432 Benzidine 92875 Benzotrichloride 98077 Benzyl chloride 100447 Biphenyl 92524 Bis(2-ethylhexyl)phthalate (DEHP) 117817 Bis(chloromethyl)ether 542881 Bromoform 75252 1,3-Butadiene 106990 Calcium cyanamide 156627 Captan 133062 Carbaryl 63252 Carbon disulfide 75150 Carbon tetrachloride 56235 Carbonyl sulfide 463581 Catechol 120809 Chloramben 133904 Chlordane 57749 Chlorine 7782505 Chloroacetic acid 79118 2-Chloroacetophenone 532274 Chlorobenzene 108907 Chlorobenzilate 510156 Chloroform 67663 Chloromethyl methyl ether 107302 Chloroprene 126998 Cresols/Cresylic acid (isomers and mixture) 1319773 o-Cresol 95487 m-Cresol 108394 p-Cresol 106445 Cumene 98828 2,4-D, salts and esters 94757 DDE 3547044 Diazomethane 334883 Dibenzofurans 132649 1,2-Dibromo-3-chloropropane 96128 Dibutylphthalate 84742 1,4-Dichlorobenzene(p) 106467 3,3-Dichlorobenzidene 91941 Dichloroethyl ether (Bis(2-chloroethyl)ether) 111444 1,3-Dichloropropene 542756 Dichlorvos 62737 Diethanolamine 111422 N,N-Diethyl aniline (N,N-Dimethylaniline) 121697 List of Hazardous Air Pollutants (HAP)Pollutant Name CAS No. List of Hazardous Air Pollutants (HAP) Diethyl sulfate 64675 3,3-Dimethoxybenzidine 119904 Dimethyl aminoazobenzene 60117 3,3'-Dimethyl benzidine 119937 Dimethyl carbamoyl chloride 79447 Dimethyl formamide 68122 1,1-Dimethyl hydrazine 57147 Dimethyl phthalate 131113 Dimethyl sulfate 77781 4,6-Dinitro-o-cresol, and salts 534521 2,4-Dinitrophenol 51285 2,4-Dinitrotoluene 121142 1,4-Dioxane (1,4-Diethyleneoxide) 123911 1,2-Diphenylhydrazine 122667 Epichlorohydrin (l-Chloro-2,3-epoxypropane) 106898 1,2-Epoxybutane 106887 Ethyl acrylate 140885 Ethyl benzene 100414 Ethyl carbamate (Urethane) 51796 Ethyl chloride (Chloroethane) 75003 Ethylene dibromide (Dibromoethane) 106934 Ethylene dichloride (1,2-Dichloroethane) 107062 Ethylene glycol 107211 Ethylene imine (Aziridine) 151564 Ethylene oxide 75218 Ethylene thiourea 96457 Ethylidene dichloride (1,1-Dichloroethane) 75343 Formaldehyde 50000 Heptachlor 76448 Hexachlorobenzene 118741 Hexachlorobutadiene 87683 Hexachlorocyclopentadiene 77474 Hexachloroethane 67721 Hexamethylene-1,6-diisocyanate 822060 Hexamethylphosphoramide 680319 Hexane 110543 Hydrazine 302012 Hydrochloric acid 7647010 Hydrogen fluoride (Hydrofluoric acid) 7664393 Hydrogen sulfide 7783064 Hydroquinone 123319 Isophorone 78591 Lindane (all isomers) 58899 Maleic anhydride 108316 Methanol 67561 Methoxychlor 72435 Methyl bromide (Bromomethane) 74839 Methyl chloride (Chloromethane) 74873 Methyl chloroform (1,1,1-Trichloroethane) 71556 Methyl hydrazine 60344 Methyl iodide (Iodomethane) 74884 Methyl isobutyl ketone (Hexone) 108101 Methyl isocyanate 624839 Methyl methacrylate 80626 Methyl tert butyl ether 1634044 4,4-Methylene bis(2-chloroaniline) 101144 Methylene chloride (Dichloromethane) 75092 Methylene diphenyl diisocyanate (MDI) 101688 4,4'¬-Methylenedianiline 101779 Naphthalene 91203Pollutant Name CAS No. List of Hazardous Air Pollutants (HAP) Nitrobenzene 98953 4-Nitrobiphenyl 92933 4-Nitrophenol 100027 2-Nitropropane 79469 N-Nitroso-N-methylurea 684935 N-Nitrosodimethylamine 62759 N-Nitrosomorpholine 59892 Parathion 56382 Pentachloronitrobenzene (Quintobenzene) 82688 Pentachlorophenol 87865 Phenol 108952 p-Phenylenediamine 106503 Phosgene 75445 Phosphine 7803512 Phosphorus 7723140 Phthalic anhydride 85449 Polychlorinated biphenyls (Aroclors) 1336363 1,3-Propane sultone 1120714 beta-Propiolactone 57578 Propionaldehyde 123386 Propoxur (Baygon) 114261 Propylene dichloride (1,2-Dichloropropane) 78875 Propylene oxide 75569 1,2-Propylenimine (2-Methyl aziridine) 75558 Quinoline 91225 Quinone 106514 Styrene 100425 Styrene oxide 96093 2,3,7,8-Tetrachlorodibenzo-p-dioxin 1746016 1,1,2,2-Tetrachloroethane 79345 Tetrachloroethylene (Perchloroethylene) 127184 Titanium tetrachloride 7550450 Toluene 108883 2,4-Toluene diamine 95807 2,4-Toluene diisocyanate 584849 o-Toluidine 95534 Toxaphene (chlorinated camphene) 8001352 1,2,4-Trichlorobenzene 120821 1,1,2-Trichloroethane 79005 Trichloroethylene 79016 2,4,5-Trichlorophenol 95954 2,4,6-Trichlorophenol 88062 Triethylamine 121448 Trifluralin 1582098 2,2,4-Trimethylpentane 540841 Vinyl acetate 108054 Vinyl bromide 593602 Vinyl chloride 75014 Vinylidene chloride (1,1-Dichloroethylene) 75354 Xylenes (isomers and mixture) 1330207 o-Xylenes 95476 m-Xylenes 108383 p-Xylenes 106423 Antimony Compounds 0 Arsenic Compounds (inorganic including arsine) 0 Beryllium Compounds 0 Cadmium Compounds 0 Chromium Compounds 0 Cobalt Compounds 0 Coke Oven Emissions 0Pollutant Name CAS No. List of Hazardous Air Pollutants (HAP) Cyanide Compounds 0 Glycol ethers 0 Lead Compounds 0 Manganese Compounds 0 Mercury Compounds 0 Fine mineral fibers 0 Nickel Compounds 0 Polycylic Organic Matter 0 Radionuclides (including radon) 0 Selenium Compounds 0

# Other ICR Response Info.

## ELECTRONIC CODE OF FEDERAL REGULATIONS e-CFR Data is current as of April 29, 2013

Title 40: Protection of Environment PART 63—NATIONAL EMISSION STANDARDS FOR HAZARDOUS AIR POLLUTANTS FOR SOURCE CATEGORIES (CONTINUED) Subpart PP—National Emission Standards for Containers § 63.923 Standards—Container Level 2 controls. (a) This section applies to owners and operators subj ect to this subpart and required to control air emissions from containers using Container Level 2 controls. (b) A container using Container Level 2 controls is one of the following: (1) A container that meets the applicable U.S. D epartment of Transportation (DOT) regulations on packaging hazardous materials for transportation asspecified in paragraph (f) of this section. (2) A container that has been demonstrated to operate with no detectable organic emissions as defined in § 63.921 of this subpart. (3) A container that has been demonstrated within the preceding 12 months to be vapor-tight by using Method 27 in appendix A of 40 CFR part 60 in accordance with the procedure specified in § 63.925(b) of this subpart. (c) Transfer of regulated-material in to or out of a container using Container Level 2 controls shall be conducted in such a manner as to minimize exposure of the regulated-material to the atmosphere, to the extent practical, considering the physi cal properties of the regulated-material and good engineering and safety practices for handling flammabl e, ignitable, explosive, or other hazardous materials. Examples of contai ner loading procedures that meet the requirements of this paragraph include using any one of the following: a submerged-fill pipe or other submerged-fill method to load liquids into the container; a vapor-balancing system or a vapor-recovery system to collect and control the vapors displaced from the container during fill ing operations; or a fitted opening in the top of a container through which the regulated-material is filled, with subsequent purging of the transfer line before removing it from the container opening. (d) Whenever a regulated-material is in a containerusing Container Level 2 controls, the owner or operator shall install all covers and closure devices for the container, and secure and maintain each closure device in the closed position except as follows: (1) Opening of a closure device or cover is al lowed for the purpose of adding material to the container as follows: (i) In the case when the container is filled tothe intended final level in one continuous operation, the owner or operator shall promptly secure the cl osure devices in the closed position and install the covers, as applicable to the container, upon conclusion of the filling operation. 

### Page 1 of 3 eCFR — Code of Federal Regulations

5/1/2013 http ://www.ecfr. gov/cgi-bin/text-idx?c=ecfr&SID=907066c5e04ce3c78ec41a430b5b0c3e&rgn=div8&vie

...

### (ii) In the case when discrete quantities or batches of material intermittently are added to the container over a period of time, the owner or operatorshall promptly secure the closure devices in the closed position and install covers, as applicable to t he container, upon either the container being filled to the intended final level, the completion of a batch loading after which no additional material will be added to the container within 15 minutes, the person performing the loading operation leaves the immediate vicinity of the container, or the s hutdown of the process generating the material being added to the container, whichever condition occurs first. (2) Opening of a closure device or cover is allowed for the purpose of removing material from the container as follows: (i) For the purpose of meeting the requirements of this section, an empty container as defined in § 63.921 of this subpart may be open to the atmosphere at any time (e.g., covers and closure devices are not required to be secured in the closed position on an empty container). (ii) In the case when discrete quantities or batchesof material are removed from the container but the container does not meet the conditions to be an empty container as defined in § 63.921 of this subpart, the owner or operator shall promptly secu re the closure devices in the closed position and install covers, as applicable to the container, upon the completion of a batch removal after which no additional material will be removed from the container within 15 minutes or the person performing the unloading operation leaves the immediate vicinity ofthe container, whichever condition occurs first. (3) Opening of a closure device or cover is allowed when access inside the container is needed to perform routine activities other than transfer of regulated-material. Examples of such activities include those times when a worker needs to open a port to measure the depth of or sample the material in the container, or when a worker needs to open a manhole hatch to access equipment inside the container. Following completion of the activity, the owner or operator shall promptly secure the closure device in the closed position or reinstall the cover, as applicable to the container. (4) Opening of a spring-loaded pressure-vacuum relief valve, conservation vent, or similar type of pressure relief device which vents to the atmosphere is allowed during normal operations for the purpose of maintaining the container internal pressure in accordance with the container design specifications. The device shall be designed to operate with no detectable organic emissions when the device is secured in the closed position. The setti ngs at which the device opens shall be established such that the device remains in the closed position whenever the container internal pressure is within the internal pressure operating range determined by the owner or operator based on container manufacturer recommendations, applicable regulations, fire protection and prevention codes, standard engineering codes and practices, or other requi rements for the safe handling of flammable, combustible, explosive, reactive, or hazardous materials. Examples of normal operating conditions that may require these devices to open are during t hose times when the container internal pressure exceeds the internal pressure operating range for t he container as a result of loading operations or diurnal ambient temperature fluctuations. (5) Opening of a safety device, as defined in § 63.921 of this subpart, is allowed at any time conditions require it to do so to avoid an unsafe condition. (e) The owner or operator shall inspect containers using Container Level 2 controls in accordance with the procedures specified in § 63.926(a) of this subpart. (f) For the purpose of compliance with paragraph (b)(1) of this section, containers shall be used that meet the applicable U.S. DOT regulations on packaging hazardous materials for transportation as follows: (1) The container meets the applicable requirements specified in 49 CFR part 178—Specifications for Packagings or 49 CFR part 179—Specifications for Tank Cars. 

### Page 2 of 3 eCFR — Code of Federal Regulations

5/1/2013 http ://www.ecfr. gov/cgi-bin/text-idx?c=ecfr&SID=907066c5e04ce3c78ec41a430b5b0c3e&rgn=div8&vie

...For questions or comments regarding e-CFR editorial content, features, or design, email 

### ecfr@nara.gov

. For questions concerning e-CFR programming and delivery issues, email 

### webteam@gpo.gov

. 

### (2) Regulated-material is managed in the container in accordance with the applicable requirements specified in 49 CFR part 107 subpart B—Exemptions; 49 CFR part 172—Hazardous Materials Table, Special Provisions, HazardousMaterials Communications, Emergency Response Information, and Training Requirements; 49 CF R part 173—Shippers—General Requirements for Shipments and Packaging; and 49 CFR part 180—Continuing Qualification and Maintenance of Packagings. (3) For the purpose of complying with this subpart, no exceptions to the 49 CFR part 178 or part 179 regulations are allowed except as provided for in paragraph (f)(4) of this section. (4) For a lab pack that is managed in accordance with the requirements of 49 CFR part 178 for the purpose of complying with this subpart, an owner or operator may comply with the exceptions for those packagings specified in 49 CFR 173.12(b). 

### Page 3 of 3 eCFR — Code of Federal Regulations

5/1/2013 http ://www.ecfr. gov/cgi-bin/text-idx?c=ecfr&SID=907066c5e04ce3c78ec41a430b5b0c3e&rgn=div8&vie

...

## ELECTRONIC CODE OF FEDERAL REGULATIONS e-CFR Data is current as of April 29, 2013

Title 40: Protection of Environment PART 63—NATIONAL EMISSION STANDARDS FOR HAZARDOUS AIR POLLUTANTS FOR SOURCE CATEGORIES (CONTINUED) Subpart PP—National Emission Standards for Containers § 63.922 Standards—Container Level 1 controls. (a) This section applies to owners and operators subj ect to this subpart and required to control air emissions from containers using Container Level 1 controls. (b) A container using Container Level 1 controls is one of the following: (1) A container that meets the applicable U.S. D epartment of Transportation (DOT) regulations on packaging hazardous materials for transportation asspecified in paragraph (f) of this section. (2) A container equipped with a cover and closure devices that form a continuous barrier over the container openings such that when the cover and clos ure devices are secured in the closed position there are no visible holes, gaps, or other open spaces into the interior of the container. The cover maybe a separate cover installed on the container (e.g., a lid on a drum, a suitably secured tarp on a rolloff box) or may be an integral part of the container structural design (e.g., a bulk cargo container equipped with a screw-type cap). (3) An open-top container in which an organic vapor-suppressing barrier is placed on or over the regulated-material in the container such that no re gulated-material is exposed to the atmosphere. One example of such a barrier is application ofa suitable organic-vapor suppressing foam. (c) A container used to meet the requirements of either paragraph (b)(2) or (b)(3) of this section shall be equipped with covers and closure devices, asapplicable to the container, that are composed of suitable materials to minimize exposure of the regulated-material to the atmosphere and to maintain the equipment integrity for as long as it is in service. Factors to be considered when selecting the materials for and designing the cover and closure devices shall include: organic vapor permeability, the effects of contact with the material or its vapor managed in the container; the effects of outdoor exposure to wind, moisture, and sunlight; and the operating practices used for container on which the cover is installed. (d) Whenever a regulated-material is in a containerusing Container Level 1 controls, the owner or operator shall install all covers and closure devices for the container, and secure and maintain each closure device in the closed position except as follows: (1) Opening of a closure device or cover is al lowed for the purpose of adding material to the container as follows: (i) In the case when the container is filled tothe intended final level in one continuous operation, the owner or operator shall promptly secure the cl osure devices in the closed position and install the covers, as applicable to the container, upon conclusion of the filling operation. 

### Page 1 of 3 eCFR — Code of Federal Regulations

5/1/2013 http ://www.ecfr. gov/cgi-bin/text-idx?c=ecfr&SID=907066c5e04ce3c78ec41a430b5b0c3e&rgn=div8&vie

...

### (ii) In the case when discrete quantities or batches of material intermittently are added to the container over a period of time, the owner or operatorshall promptly secure the closure devices in the closed position and install covers, as applicable to t he container, upon either: the container being filled to the intended final level; the completion of a batch loading after which no additional material will be added to the container within 15 minutes; the person performing the loading operation leaves the immediate vicinity of the container; or the s hutdown of the process generating the material being added to the container, whichever condition occurs first. (2) Opening of a closure device or cover is allowed for the purpose of removing material from the container as follows: (i) For the purpose of meeting the requirements of this section, an empty container as defined in § 63.921 of this subpart may be open to the atmosphere at any time (e.g., covers and closure devices are not required to be secured in the closed position on an empty container). (ii) In the case when discrete quantities or batchesof material are removed from the container but the container does not meet the conditions to be an empty container as defined in § 63.921 of this subpart, the owner or operator shall promptly secu re the closure devices in the closed position and install covers, as applicable to the container, upon the completion of a batch removal after which no additional material will be removed from the container within 15 minutes, or the person performing the unloading operation leaves the immediate vicinity ofthe container, whichever condition occurs first. (3) Opening of a closure device or cover is allowed when access inside the container is needed to perform routine activities other than transfer of regulated-material. Examples of such activities include those times when a worker needs to open a port to measure the depth of or sample the material in the container, or when a worker needs to open a manhole hatch to access equipment inside the container. Following completion of the activity, the owner or operator shall promptly secure the closure device in the closed position or reinstall the cover, as applicable to the container. (4) Opening of a spring-loaded pressure-vacuum relief valve, conservation vent, or similar type of pressure relief device which vents to the atmosphere is allowed during normal operations for the purpose of maintaining the container internal pressure in accordance with the container design specifications. The device shall be designed to operate with no detectable organic emissions when the device is secured in the closed position. The setti ngs at which the device opens shall be established such that the device remains in the closed position whenever the container internal pressure is within the internal pressure operating range determined by the owner or operator based on container manufacturer recommendations, applicable regulations, fire protection and prevention codes, standard engineering codes and practices, or other requirements for the safe handling of flammable, ignitable, explosive, reactive, or hazardous materials. Examples of normal operating conditions that may require these devices to open are during those times when the container internal pressure exceeds the internal pressure operating range for the container asa result of loading operations or diurnal ambient temperature fluctuations. (5) Opening of a safety device, as defined in § 63.921 of this subpart, is allowed at any time conditions require it to do so to avoid an unsafe condition. (e) The owner or operator shall inspect containers using Container Level 1 controls in accordance with the procedures specified in § 63.926(a) of this subpart. (f) For the purpose of compliance with paragraph (b)(1) of this section, containers shall be used that meet the applicable U.S. DOT regulations on packaging hazardous materials for transportation as follows: (1) The container meets the applicable requirements specified in 49 CFR part 178—Specifications for Packagings or 49 CFR part 179—Specifications for Tank Cars. 

### Page 2 of 3 eCFR — Code of Federal Regulations

5/1/2013 http ://www.ecfr. gov/cgi-bin/text-idx?c=ecfr&SID=907066c5e04ce3c78ec41a430b5b0c3e&rgn=div8&vie

...For questions or comments regarding e-CFR editorial content, features, or design, email 

### ecfr@nara.gov

. For questions concerning e-CFR programming and delivery issues, email 

### webteam@gpo.gov

. 

### (2) Regulated-material is managed in the container in accordance with the applicable requirements specified in 49 CFR part 107 subpart B—Exemptions; 49 CFR part 172—Hazardous Materials Table, Special Provisions, HazardousMaterials Communications, Emergency Response Information, and Training Requirements; 49 CF R part 173—Shippers—General Requirements for Shipments and Packaging; and 49 CFR part 180—Continuing Qualification and Maintenance of Packagings. (3) For the purpose of complying with this subpart, no exceptions to the 49 CFR part 178 or part 179 regulations are allowed except as provided for in paragraph (f)(4) of this section. (4) For a lab pack that is managed in accordance with the requirements of 49 CFR part 178 for the purpose of complying with this subpart, an owner or operator may comply with the exceptions for those packagings specified in 49 CFR 173.12(b). 

### Page 3 of 3 eCFR — Code of Federal Regulations

5/1/2013 http ://www.ecfr. gov/cgi-bin/text-idx?c=ecfr&SID=907066c5e04ce3c78ec41a430b5b0c3e&rgn=div8&vie

...

## ELECTRONIC CODE OF FEDERAL REGULATIONS e-CFR Data is current as of April 29, 2013

Title 40: Protection of Environment PART 63—NATIONAL EMISSION STANDARDS FOR HAZARDOUS AIR POLLUTANTS FOR SOURCE CATEGORIES (CONTINUED) Subpart DD—National Emission Standards for Hazardous Air Pollutants from Off-Site Waste and Recovery Operations § 63.689 Standards: Transfer systems. (a) The provisions of this section apply to the control of air emissions from transfer systems for which § 63.683(b)(1)(i) of this subpart references the use of this section for such air emission control. (b) For each transfer system that is subject to th is section and is an individual drain system, the owner or operator shall control air emissions in accordance with the standards specified in 40 CFR part 63, subpart RR—National Emission Standards for Individual Drain Systems. (c) For each transfer system that is subject to thissection but is not an individual drain system, the owner or operator shall control air emissions byusing one of the transfer systems specified in paragraphs (c)(1) through (c)(3) of this section. (1) A transfer system that uses covers in accordance with the requirements specified in paragraph (d) of this section. (2) A transfer system that consists of continuous hard-piping. All joints or seams between the pipe sections shall be permanently or semi-permanently sealed (e.g., a welded joint between two sections of metal pipe or a bolted and gasketed flange). (3) A transfer system that is enclosed and vented through a closed-vent system to a control device in accordance with the requirements specif ied in paragraphs (c)(3)(i) and (c)(3)(ii) of this section. (i) The transfer system is designed and operated such that an internal pressure in the vapor headspace in the enclosure is maintained at a level less than atmospheric pressure when the control device is operating, and (ii) The closed-vent system and control device are designed and operated in accordance with the requirements of § 63.693 of this subpart. (d) Owners and operators controlling air emissionsfrom a transfer system using covers in accordance with the provisions of paragraph (c)(1) of this section shall meet the requirements specified in paragraphs (d)(1) through (d)(6) of this section. (1) The cover and its closure devices shall be designed to form a continuous barrier over the entire surface area of the off-site material as it is conveyed by the transfer system except for the openings at the inlet and outlet to the transfer system through which the off-site material passes. The 

### Page 1 of 2 eCFR — Code of Federal Regulations

5/1/2013 http ://www.ecfr. gov/cgi-bin/text-idx?c=ecfr&SID=907066c5e04ce3c78ec41a430b5b0c3e&rgn=div8&vie

...For questions or comments regarding e-CFR editorial content, features, or design, email 

### ecfr@nara.gov

. For questions concerning e-CFR programming and delivery issues, email 

### webteam@gpo.gov

. 

### inlet and outlet openings used for passage of the off-site material through the transfer system shall be the minimum size required for practical operation of the transfer system. (2) The cover shall be installed in a manner such that there are no visible cracks, holes, gaps, or other open spaces between cover section joints or between the interface of the cover edge and its mounting. (3) Except for the inlet and outlet openings to the transfer system through which the off-site material passes, each opening in the cover s hall be equipped with a clos ure device designed to operate such that when the closure device is secured in the closed position there are no visible cracks, holes, gaps, or other open spaces in the closure device or between the perimeter of the opening and the closure device. (4) The cover and its closure devices shall be made of suitable materials that will minimize exposure of the off-site material to the atmosphere, to the extent practical, and will maintain the integrity of the equipment throughout its intended serv ice life. Factors to be considered when selecting the materials for and designing the cover and closure devices shall include: organic vapor permeability; the effects of any contact with the material or its vapors conveyed in the transfer system; the effects of outdoor exposure to wind, moisture, and sunlight; and the operating practices used for the transfer system on which the cover is installed. (5) Whenever an off-site material is in the transfer system, the cover shall be installed with each closure device secured in the closed position except asspecified in paragraph (d)(5)(i) or (d)(5)(ii) of this section. (i) Opening of closure devices or removal of the cover is allowed to provide access to the transfer system for performing routine inspection, mainten ance, repair, or other activities needed for normal operations. Examples of such activities include those times when a worker needs to open a hatch or remove the cover to repair conveyance equipment m ounted under the cover or to clear a blockage of material inside the system. Following completion of t he activity, the owner or operator shall promptly secure the closure device in the closed position or reinstall the cover, as applicable. (ii) Opening of a safety device, as defined in § 63.681 of this subpart, is allowed at any time conditions require it to do so to avoid an unsafe condition. (6) The owner or operator shall inspect the air emission control equipment in accordance with the requirements specified in § 63.695 of this subpart. [61 FR 34158, July 1, 1996, as amen ded at 64 FR 38970, July 20, 1999] 

### Page 2 of 2 eCFR — Code of Federal Regulations

5/1/2013 http ://www.ecfr. gov/cgi-bin/text-idx?c=ecfr&SID=907066c5e04ce3c78ec41a430b5b0c3e&rgn=div8&vie

...Co. ID: 2052 Site ID: 10725 Emission Factors 

## Bituminous and Subbituminious Coal Comustion AP-42 Table 1.1-3 Emission Factors for Sox, Nox, and CO from Bituminous and Subbituminous Coal Computstion

38 S

38 S

38 S

35 S

35 S

38 S

35 S

38 S

38 S

38 S 

## Clean Harbors Aragonite

Firing Configuration SCC Sox Nox CO Emission Factor (lb/ton) EMISSION FACTOR RATING Emission Factor (lb/ton) EMISSION FACTOR RATING

11 A 0.5 A 1-02-002-02 1-03-002-06 1-03-002-06PC, dry bottom, wallfired bituminous PreNSPS with low -Nox burner 1-01-002-02 A Emission Factor (lb/ton) EMISSION FACTOR RATINGPC, dry bottom, wallfired, bituminous PreNSPS 1-01-002-02 A 22 A 0.5 A 1-02-002-02

1-02-002-22 1-03-002-22
PC, drybottom, wallfired, subbituminous NSPS 1-01-002-22 

### A 7.4 A 1-02-002-02 1-03-002-06PC, dry bottom wallfired, subbituminous PreNSPS 1-01-002-22 A 12 C 0.5 APC, dry bottom wallfired, bituminous NSPS 1-01-002-02 A 12 A 0.5

0.5 A

PC, dry bottom, cellburner fired, subbituminous 1-01-002-35 A 14 E 0.5 A 0.5 A 1-02-002-22 1-03-002-22 PC, drybottom, cell burner fired, bituminous 1-01-002-15 A 31 A

A 0.5 A 1-02-002-12 1-03-002-16 1-03-002-16

PC, dry bottom, Tangentially fired,bituminous, PreNSPS with low-Nox burner 1-01-002-12 A 9.7 A

PC, dry bottom, tangentially fired,bituminous, PreNSPS 1-01-002-12 A 15 A 0.5 A 1-02-002-12

A PC, dry bottom, 1-01-002-12 10 A 0.535 S

35 S

38 S

38 S

35 S

38 S

35 S

38 S

35 S

38 S 35 S

31 S

31 S 5 18

15.2 18 A 0.5 A 1-02-002-26 1-03-002-26

PC, wet bottom, wallfired, bituminous, Pre-NSPS 1-01-002-01 A 31 D 1-02-002-26 1-03-002-26

PC, dry bottom, tangentially fired, sub-bituminous, NSPS 1-01-002-26 

### A 7.2 1-02-002-12 1-03-002-16 PC, dry bottom, tangentially fired,sub-bituminous, PreNSPS 1-01-002-26 A 8.4 A 0.5 A , y , tangentially fired, bituminous, NSPS

A

PC, wet bottom, wallfired sub-bituminous 1-01-002-21 A 24 E 0.5 A 1-02B002-21 1-03-002-21 0.5 A 1-02-002-01 1-03-002-05 PC, wet bottom, tangentially fired, bituminous, NSPS 1-01-002-11 A 14 E 0.5

1-02-002-23 1-03-002-23 Spreader Stoker, bituminous 1-02-002-04 A 1-02-002-03 1-03-002-03 Cyclone Furnace, subbituminous 1-01-002-23 A 17 C 0.5 A Cyclone Furnace, bituminous 1-01-002-03 A 33 A 0.5

5 A 1-02-002-24 1-03-002-24 Overfeed Stoker 1-01-002-05/25 B 7.5 A 6 1-03-002-09Spreader Stoker, subbituminous 1-01-002-24 B 8.8 B 1-01-002-04 B 11 B 5 A

1-02-002-06 B 9.5 A 11 B B 1-02-002-05/25 1-03-002-07/25 Underfeed Stoker

1-02-002-18 1-03-002-18 9.1 E 275 E FBC, circulation bed 1-01-002-18 C E D E 1-03-002-08 Hand-fed Units 1-03-002-14 D

1-02-002-17 1-03-002-17 FBC, bubbling bed 1-01-002-17 C E D D10 A A 2.3 A E

10 A B 2.3 A E

7 A D 2.6 A E

2 A E 0.26 A E

B E

B E

A E

C E

C E

D E

D E

E E
E E

E E AP-42 Table 1.1-4 Uncontrolled Emission Factor for PM and PM-10 From Bituminous and Subbituminous Coal Combustion

Firing Configuration SCC Filterable PM Filterable PM
Emission Factor EMISSION FACTOR RATING Emission Factor

PC-fired, wet bottom 1-01-002-01/21 1-02-002-01/21 1-03-002-05/21 1-03-002-06/22 PC-fired, dry bottom,

tangentially fired 1-01-002-12/26 1-02-002-12/26 1-03-002-16/26 EMISSION FACTOR RATING (lb/ton) (lb/ton)
PC- fired, dry bottom, wall-fired 1-01-002-02/22 1-02-002-02/22

1-03-002-09/24
Spreader Stoker, with multiple cyclones, no reinjection 1-01-002-04/24 12 66 13.2 1-02-002-04/24 1-03-002-09/24 Spreader stoker, with multiple cyclones, and reinjection 1-01-002-04/24 17 12.4 1-02-002-04/24 Cyclone furnace 1-01-002-03/23 1-02-002-03/23 1-03-002-03/23 Spreader Stoker 1-01-002-04/24

5.0 1-02-002-05/25 1-03-002-07/25 Underfeed stoker 1-02-002-06 15 6.2 1-02-002-05/25 1-03-002-07/25 Overfeed Stoker, with multiple cyclones 1-01-002-05/25 9 7.8 1-02-002-04/24 1-03-002-09/24 Overfeed Stoker 1-01-002-05/25 16 6.0

1-02-002-17 1-03-002-17 FBC, circulating bed 1-01-002-18 Hand-fed units 1-03-002-14 15 6.2 FBC, bubbling bed 1-01-002-17 1-03-002-08 Underfeed stoker, with multiple cyclone 1-02-002-06 11 6.2 1-03-002-08

1-02-002-180.1-0.3 S B E E

0.02 E ND ND

0.04 C E E

AP-42 Table 1.1-6 Cumulative Particle Size Distribution and Size-Specific Emission Factors for Dry Bottom Boilers Burning Pulverized Bituminous and Subbituminous Coal

15 54 81 79 97 3.2 A 1.08 A 0.48 A 0.064 A 0.02 A 10 29 71 67 92 2.3 A 0.58 A 0.42 A 0.054 A 0.02 A 6 14 62 50 77 1.7 A 0.28 A 0.38 A 0.024 A 0.02 A 2.5 3 51 29 53 0.6 A 0.06 A 0.3 A 0.024 A 0.01 A 1.25 1 35 17 31 0.2 A 0.02 A 0.22 A 0.01 A 0.006 A

1 1 31 14 25 0.2 A 0.02 A 0.18 A 0.01 A 0.006 A 0.625 1 20 12 14 0.1 A 0.02 A 0.12 A 0.01 A 0.002 A TOTAL 100 100 100 100 10 A 2 A 0.6 A 0.08 A 0.02 A EMISSION FACTOR RATING Emission Factor (lb/MMBtu) EMISSION FACTOR RATINGAll pulverized Coalfired boilers All PM controls (without FGD controls) 1-01-002-01/21 80% of CPMTOT emission 20% of CPM-TOT emission factor 1-03-002-18 AP-42 Table 1.1-5 Condensable Particulate Matter Emission Factors For Bituminous and Subbituminous Coal Combustion

Firing Configuration Controls SCC CPM - TOT CPM - IOR CPM - ORG
Emission Factor (lb/MMBtu)

1-03-002-16 1-03-002-21/22

1-03-002-26All pulverized coalfired boilers All PM controls combined with an FGD control 1-01-002-01/21 1-01-002-02/22 1-01-002-12-26 1-01-002-02/22 1-01-002-12/26 1-02-002-01/21 1-02-002-02/22 1-02-002-12/26 1-03-002-05/06 EMISSION FACTOR RATING Emission Factor (lb/MMBtu)

20% of CPM-TOT emission factor 1-01-002-05/25 1-02-002-04/24 1-02-002-05/25

1-02-002-06 1-03-002-07/08

1-03-002-26 Spreader stoker, travelling grate overfeed stoker, underfeed stoker All PM controls, or Uncontrolled 1-01-002-04/24 TOT emission factor 1-02-002-01/21 1-02-002-02/22 1-02-002-12/26 1-03-002-05/06

1-03-002-16 1-03-002-21/22

ESP Baghouse 32 23 17 Cumulative Emission Factor (lb/ton)

Uncontrolled Controlled
Uncontrolled Controlled Multiple Cyclones Scrubber ESP Baghouse Multiple Cyclones 1-03-002-09/11

1-03-002-16 1-03-002-24/25

Cumulative Mass % <Stated Size

EMISSION FACTOR RATING: E 6 2 2 1 100 AP-42 1.1-7 Cumulative Particle Size Distribution and Size-Specific Emission Factors for Wet Bottom Boilers Burning Pulverized Bituminous Coal Scrubber

Particle Size (um)15 83 2.8 A 1.38 A 0.046 A 10 75 2.6 A 1.3 A 0.042 A 6 63 2.32 A 1.18 A 0.036 A 2.5 40 1.48 A 0.86 A 0.022 A 1.25 17 0.42 A 0.44 A 0.01 A

1 8 0.28 A 0.26 A 0.004 A 0.625 0.14 A TOTAL 100 7 A 1.4 A 0.056 A

15 90 0.66 A 0.114 A 0.013 A 10 68 0.26 A 0.112 A 0.011 A 6 56 0.16 A 0.112 A 0.009 A 2.5 36 0.11 A 0.11 A 0.006 A 1.25 22 0.1 A 0.1 A 0.004 A

1 17 0.1 A 0.1 A 0.003 A 0.625 0 TOTAL 100 2 A 0.12 A 0.016 A AP-42 Table 1.1-9 Cumulative Particle Size Distribution and Size-Specific Emission Factors For Spreader Stokers Burning Bituminous Coal

15 86 74 97 72 14.6 8.8 0.46 0.086 10 73 65 90 60 12 7.8 0.44 0.072 6 51 52 82 46 8.6 6.2 0.4 0.056 2.5 8 27 61 26 1.4 3.2 0.3 0.032 1.25 2 16 46 18 0.4 2 0.22 0.022

1 2 14 41 15 0.4 1.6 0.2 0.018 0.625 1 9 C 7 0.2 1 C 0.006 TOTAL 100 100 100 100 17 12 0.48 0.12

15 7.8 C 5.4 E 10 6 C 5 E 6 3.8 C 4.4 E 2.5 2.2 C 3.8 E 1.25 2 C 3.6 E Particle Size (um) Cumulative Mass % <Stated Size Cumulative Emission Factor (lb/ton)

Uncontrolled Controlled Uncontrolled Controlled Multiple Cyclones ESP

4 19 2 100 100 33 84 21 61 6 31 Multiple Cyclones ESP 40 99 37 93

ESP Multiple Cyclones ESP 33 95 13 94 AP-42 1.1-8 Cumulative Size Distribution and Size-Specific Emission Factors for Cyclone Furnaces Buring Bituminous Coal EMISSION FACTOR RATING: E

Particle Size (um) Cumulative Mass % <Stated Size Cumulative Emission Factor (lb/ton)

Uncontrolled Controlled
Uncontrolled Controlled Multiple Cyclones

Particle Size (um) Cumulative Mass % <Stated Size Cumulative Emission Factor (lb/ton)

Uncontrolled Controlled Uncontrolled Controlled Multiple Cyclones Multiple Cyclones ESP 5 82 0 100 100

8 93 5.5 92

5 85

5 3.3 5 3.3 4 2.6 20 13.2 14 9.2 7 4.6 Baghouse ple Cyclo Cyclone s ESP Baghouse 28 18.5

37 55 24 49 14 43 Emission Factor EMISSION FACTOR RATING Emission Factor EMISSION FACTOR RATING 49 60 100 66 AP-42 1.1-10 Cumulative Particle Size Distribution and Size-Specific Emission Factors For Overfeed Stokers Burning Bituminous Coal

Particle Size (um) Cumulative Mass % <Stated Size Cumulative Emission Factor (lb/ton)

Uncontrolled Multiple Cyclones Controlled Uncontrolled Multiple Cyclones Controlled

13 391 2 C 3.6 E 0.625 1.4 E TOTAL 16 C 9 E

PC-fired, dry bottom

PC-fired, dry bottom, tangential

PC-fired, wet bottom

Cyclone Furnace

Spreader Stoker

Overfeed Stoker

Underfeed Stoker
FBC, Bubbling Bed

FBC, Circulation Bed 15 50 7.6 10 41 6.2 100 100 AP-42 1.1-11 Cumulative Particle Size Distribution and Size-Specific Emission Factors for Underfeed Stokers Burning Bituminous Coal EMISSION FACTOR RATING: C

Particle Size (um) Cumulative Mass % <Stated Size Uncontrolled Cumulative Emission Factor (lb/ton) 12 39 16

0.625 18 2.7 TOTAL 100 15

1.25 22 3.4

1 21 3.2 6 32 4.8 2.5 25 3.8

1-03-002-06/22 1-01-002-02/22 1.2 0.15 1-02-002-02/22 AP-42 1.1-15 Emission Factors For Hydrogen Chloride (HCl) And Hydrogen Fluoride (HF) From Coal Combustion Emission Factor Rating: B HCl HF Firing Configuration SCC Emission Factor (lb/ton) Emission Factor (lb/ton)

1-01-002-01/21 1.2 0.15 1-02-002-01/21 1-03-002-16/26 1-01-002-12/26 1.2 0.15 1-02-002-12/26

1-03-002-03/23 1-01-002-03/23 1.2 0.15 1-02-002-03/23 1-03-002-05/21

1-01-002-05/25 1.2 0.15 1-02-002-05/25 1-03-002-09/24 1-01-002-04/24 1.2 0.15 1-02-002-04/24

1-01-002-17 1.2 0.15 1-02-002-06 1.2 0.15 1-03-002-08 1-03-002-07/25

1-02-002-18 1-03-002-18 1-01-002-18/38 1.2 0.15

1-02-002-17 1-03-002-17Hand-fired Table 1.1-16 Emission Factor Equations for Trace Elements form Coal Combustion



### 0.92 *(C/A*PM)^ 0.63

3.1 *(C/A*PM)^ 0.85 1.2 *(C/A*PM)^ 1.10 3.3 *(C/A*PM)^ 0.50 3.7 *(C/A*PM)^ 0.58 1.7 *(C/A*PM)^ 0.69 3.4 *(C/A*PM)^ 0.80 3.8 *(C/A*PM)^ 0.60 4.4 *(C/A*PM)^ 0.48 C =concentration of metal in the coal, parts per million by weight (ppmwt). A = weight fraction of ash in the coal. For example, 10% ash is 0.1 ash fraction. PM = Site-specific emission factor for total particulate matter, lb/10^6 Btu.

Rating A A A A A D A A A A A A A

0.04 B 0.06 B 0.03 B

0.04 B 0.06 B 0.08 B

0.05 B 0.04 B 0.08 E

0.01 B 0.11 B 0.09 E Chromium

Cobalt Lead Manganese Nickel

AP-42 Table 1.1-18 Emission Factors for Trace Metals From Controlled Coal Combustion Pollutant (lb/10^12 Btu) Antimony

Arsenic Beryllium Cadmium 1-03-002-14 1.2 0.15

Emission Equation

Chromium (VI) 7.90E-05 Cobalt 1.00E-04 Lead 4.20E-04 Beryllium 2.10E-05 Cadmium 5.10E-05 Chromium 2.60E-04 Pollutant Emission Factor (lb/ton) Antimony 1.80E-05

Arsenic 4.10E-04

Emission Factor (lb/ton) EMISSION FACTOR RATING Emission Factor (lb/ton) EMIS SION FACT Nickel 2.80E-04 Selenium 1.30E-03

AP-42 Table 1.1-19 Emission Factors For CH4, TNMOC, and N2O From Bituminous and Subbituminous Coal Combustion

Firing Configuration SCC CH4 TNMOC N2O Magnesium 1.10E-02 Manganese 4.90E-04

Mercury 8.30E-05

PC-fired, dry bottom,

tangentially fired 1-01-002-12/26 1-02-002-12/26 1-03-002-16/26 PC-fired, wet bottom 1-01-002-01/21 1-02-002-01/21 1-03-002-05/21 PC-fired, dry bottom, wall fired 1-01-002-02/22 1-02-002-02/22 1-03-002-06/22 Emission Factor (lb/ton) EMISSION FACTOR RATING

Cyclone furnace 1-01-002-03/230.06 B 0.05 B 0.04 D

0.06 B 0.05 B 0.04 E

0.06 B 0.05 B 0.04 E

0.06 B 0.05 B 0.04 E

0.06 B 0.05 B 0.04 E

0.8 B 1.3 B 0.04 E

0.8 B 1.3 B 0.04 E

5 E 10 E 0.04 E
0.06 E 0.05 E 3.5 B

0.06 E 0.05 E 3.5 B



## Fuel Oil Combustion AP-42 Table 1.3-1 SO 2 NO X CO Filterable PM Spreader stoker,

with multiple cyclones, and

reinjection 1-01-002-04/24 1-02-002-04/24 1-03-002-09/24
Spreader stoker,

with multiple cycolnes, no

reinjection 1-01-002-04/24 1-02-002-04/24 1-03-002-09/24 1-02-002-03/23 1-03-002-03/23 Spreader stoker 1-01-002-04/24 1-02-002-04/24 1-03-002-09/24

Overfeed stoker,

with multiple

cycolnes 1-01-002-05/25 1-02-002-05/25 1-03/002-07/25 1-02-002-05/25 1-03-002-07/25 Overfeed Stoker 1-01-002-05/25

FBC, bubbling bed 1-01-002-17 1-02-002-17 Underfeed stoker, with multiple cyclone 1-02-002-06 1-03-002-08

Hand-fed units 1-03-002-14 Underfeed Stoker 1-02-002-06 1-03-002-08

Coal Type Average %C Conversion Factor Emission Factor (lb/ton coal) Subbituminous 66.3 72.6 4810 1-02-002-18 1-03-002-18
AP-42 1.1-20 Default CO2 Emission Factors For U.S. Coals Emission Factor Rating: C 1-03-002-17 FBC, circulating bed 1-01-002-18

Low-volatile bituminous 86.1 72.6 6250

Firing Configuration (SCC) EF (lb/103gal) EF Rating EF (lb/103gal) EF Rating EF (lb/103 gal) High-volatile bituminous 75.9 72.6 5510 Medium-volatile bituminous 83.2 72.6 6040

EF Ratin EF (lb/103gal) EF Rating Boilers > 100 10 6Btu/hrSO 2 NO X CO Filterable PM

AP-42 Table 1.3-3 A (1-01-004-01), (1-02-004-01), (1-03-004-01) No. 6 oil fired, normal firing, 157 * S A 40 B 5 A 5 A 9.19 * S + 3.22 No. 6 oil fired, normal firing 157 * S A 47

5 A 9.19 * S + 3.22 A No. 6 oil fired, tangential firing, 157 * S A 32 B (1-01-004-04) A 9.19 * S + 3.22 A low NOX burner (1-01-004-01), (1-02-004-01)

5 A 10 B (1-01-004-05), (1-02-004-04), No. 5 oil fired, normal firing 157 * S A 47 B 5 A 9.19 * S + 3.22 A No. 6 oil fired, tangential firing, 157 * S A 26 E low NOX burner (1-01-004-04)

5 A 7 B (1-01-005-04), (1-02-005-04), No. 4 oil fired, normal firing 150 * S A 47 B 5 A 10 B (1-01-004-06) No. 5 oil fired, tangential firing, 157 * S A 32 B

5 A 2 A (1-01-005-01), (1-02-005-01), (1-03-005-01) No. 2 oil fired 142 * S A 24 D 5 A 7 B (1-01-005-05) No. 4 oil fired, tangential firing, 150 * S A 32 B

Ratin g EF (lb/103gal) EF Rating Boilers < 100 10 6Btu/hr No. 6 oil fired 157 * S A 55 Firing Configuration (SCC) EF (lb/103 gal) EF Rating EF (lb/103gal) EF Rating EF (lb/103 gal)

5 A 2 A (1-01-005-01), (1-02-005-01), (1-03-005-01) No. 2 oil fired, LNB/FGR 142 * S A 10 D

5 A 9.19 * S + 3.22 A No. 5 oil fired 157 * S A 55 A (1-03-004-04) A 5 A 10 B (1-02-004-02/03), (1-03-004-02/03)

5 A 2 B (1-02-005-02/03), (1-03-005-02/03) Distillate oil fired 142 * S A 20 A 5 A 7 B (1-03-005-04) No. 4 oil fired 150 * S A 55 A

TOC Methane NMTOC Firing Configuration Emission Factor (lb/103gal) Emission Factor (lb/103gal) Emission Factor (lb/103gal) (SCC) 5 A 0.4 B (A2104004/A2104011) Residential furnace 142 * S A 18 A

No. 5 oil fired, tangential firing (1-01-004-06) 1.04 0.28 0.76 No. 4 oil fired, normal firing (1-01-005-04) 1.04 0.28 0.76 No. 6 oil fired, tangential firing (1-01-004-04) 1.04 0.28 0.76 No. 5 oil fired, normal firing (1-01-004-05) 1.04 0.28 0.76 Utility Boilers No. 6 oil fired, normal firing (1-01-004-01) 1.04 0.28 0.7615 7.59 A D 1.67 A E 10 7.17 A D 1.58 A E 6 6.42 A D 1.17 A E 2.5 4.67 A D 0.33 A E 1.25 3.25 A D 0.33 A E

1 3 A D 0.33 A E 0.625 2.5 A D NA Total 8.34 A D 1.67 A E
No. 6 oil: A = 1.12(S) + 0.37 No. 5 oil: A = 1.2 No. 4 oil: A = 0.84 AP-42 Table 1.3-6 (Particulate Matter), Distillate Oil, Industrial Boilers

AP-42 Table 1.3-7 (Particulate Matter)

6.5 * A No. 6 oil: A = 1.12(S) + 0.37 5.17 * A No. 5 oil: A = 1.2 3.67 * A No. 4 oil: A = 0.84 1.92 * A No. 2 oil: A = 0.24 1.33 * A 1.17 * A 1.08 * A 8.34 * A
AP-42 Table 1.3-10 Lead Distillate oil fired (1-02-005-01/02/03) 0.252 0.052 0.2 No. 4 oil fired (1-02-005-04) 0.252 0.052 0.2 No. 6 oil fired (1-02-004-01/02/03) 1.28 1.00 0.28 No. 5 oil fired (1-02-004-04) 1.28 1.00 0.28 No. 4 oil fired, tangential firing (1-01-005-05) 1.04 0.28 0.76 Industrial Boilers

No. 4 oil fired (1-03-005-04) 0.556 0.216 0.34 Residential furnace (A2104004/A2104011) 2.493 1.78 0.713 No. 5 oil fired (1-03-004-04) 1.605 0.475 1.13 Distillate oil fired (1-03-005-01/02/03) 0.556 0.216 0.34 Commercial/institutional/residential combustors No. 6 oil fired (1-03-004-01/02/03) 1.605 0.475 1.13

77 72 56 22 39 21 Emission Factor Emissio n Factor

Rating 91 100 86 95 Table 1.3-5. Cumulative Particle Size Distribution and Size-Specific Emission Factors for Industrial Boilers Firing Residual Oil

Particle Size (um) Cumulative Mass % <Stated Size Cumulative Emission Factor (lb/10^3 gal)

Uncontrolled Multiple Cyclone Controlled Uncontrolled Multiple Cyclone Controlled

Emission Factor Emission Factor Rating

15 

### 68 1.33 10 

### 50 1 Particulate emission factors for residual oil combustion without emission controls are, on average, a function of fuel oil grade and sulfur content where S is the weight % of sulfur in the oil. For Example, if the fuel is 1.0% sulfur, then S=1

Particle Size Cumulative Emission Factor Cumulative Mass % < Stated Size (lb/103gal) 36 21 30 100 100

0.625 

### 2 0.04 Total 

### 100 2 1.25 

### 9 0.17 1.00 

### 8 0.17

6 

### 30 0.58 2.5 

### 12 0.25

6 44 49 1.00 2.5 23 42 0.83 15 78 60 1.17 10 62 55 1.08 Particle Size Cumulative Emission Factor Cumulative Mass % < Stated Size (lb/103gal) Residual Oil Distillate Oil Residual Oil Distillate Oil

Firing Configuration (SCC) EF (lb/10 6btu) 0.625 13 35 0.67 Total 100 100 2.00 1.25 16 38 0.75 1.00 14 37 0.75

## Natural Gas Combustion AP-42 Table 1.4-1

AP-42 Table 1.4-2, Natural Gas Combustion

AP-42 Table 1.5-1 EMISSION FACTORS FOR LPG COMBUSTION

PM SO 2 0.09 S 0.09 S 0.1 S 0.1 S NO X N 20 CO 2 CO TOC CH 4 AP-42 Table 3.1-1 Distillate oil fired 0.000009 (1-01-005-01), (1-02-005-01) (1-03-005-01)

Controlled - Low NO x burners 140 84 Controlled - Flue gas recirculation 100 84 Uncontrolled (Pre-NSPS) 280 84 Uncontrolled (Post-NSPS) 190 84 NOx CO Emission Factor (lb/10 6scf) Emission Factor (lb/10 6scf) Large Wall-Fired Boilers (>100) [1-01-006-01, 1-02-006-01, 1-03-006-01]

Controlled - Flue gas recirculation 76 98 Controlled - Low NO x burners/Flue gas recirculation Controlled - Low NO x burners/Flue gas recirculation 32 84 Tangential - Fired Boilers (All Sizes) [1-01-006-04] Uncontrolled 170 24 Small Boilers (<100) [1-01-006-02, 1-02-006-02, 1-03-006-02, 1-03-006-03] Uncontrolled 100 84 Controlled - Low NO x burners 50 84

PM (Filterable) 

### 1.9 SO 2 0.6 N 2 0 (Uncontrolled) 2.2 PM (Total) 7.6 Lead 0.0005 PM (Condensable) 

### 5.7 Residential Furnaces (<0.3) [No SCC] Uncontrolled 94 40

Pollutant Emission Factor (lb/10 6scf)

Commercial Boilers Industrial Boilers Commercial Boilers (SCC 1-02-010-01) (SCC 1-03-010-01) (SCC 1-02-010-01) (SCC 1-03-010-01) N 2 0 (Controlled-low-NOx burner) 0.64 VOC 5.5

Pollutant Butane Emission Factor Propane Emission Factor (lb/10^3 gal) (lb/10^3 gal) Industrial Boilers

3.6 2.1 3.2 1.9 0.6 0.6 0.5 0.5 0.9 0.09 0.9 0.9 14300 14300 12500 12500

0.6 0.5 0.6 0.4
21 15 19 14

0.2 0.2 0.2 0.2Turbine Type Nitrogen Oxides Carbon Monoxide

AP-42 Table 3.1-2a Natural Gas-Fired Turbines Distillate Oil-Fired Turbines Pollutant

9.40E-01 *S

* S is the percent sulfur in the fuel (ex. If the sulfur content in the fuel is 3.4% then S = 3.4) Emission (Fuel Input) Rating (Fuel Input) Rating Natural Gas-Fired Turbines (lb/MMBtu) Emission Factor (lb/MMBtu)

Lean-Premix 9.90E-02 D 1.50E-02 D Distillate Oil-Fired Turbines Uncontrolled 3.20E-01 A 8.20E-02 A Water-Steam Injection 1.30E-01 A 3.00E-02 A

Landfill Gas-Fired Turbines Uncontrolled 1.40E-01 A 4.40E-01 A Uncontrolled 8.80E-01 C 3.30E-03 C Water-Steam Injection 2.40E-01 B 7.60E-02 C

(lb/MMBtu) Emission Factor (lb/MMBtu) Emission Factor (Fuel Input) Rating (Fuel Input) Rating Digester Gas-Fired Turbines Uncontrolled 1.60E-01 D 1.70E-02 D

Lead ND NA 1.40E-05 C SO 2 * B 1.01E+00 B CO 2 1.10E+02 A 157 A N 2 O 3.00E-03 E ND NA

VOC 2.10E-03 D 4.10E-04 E TOC 1.10E-02 B 4.00E-03 C Methane 8.60E-03 C ND NA

PM (total) 6.60E-03 C 1.20E-02 C

AP-42 Table 3.2-1. UNCONTROLLED EMISSIONS FACTORS FOR 2+B52-STROKE RICHBURN ENGINES (SCC 2-02-002-52) AP-42 Table 3.2-2. UNCONTROLLED EMISSIONS FACTORS FOR 4- STROKE LEAN-BURN ENGINES (SCC 2-02-002-54) PM (condensable) 4.70E-03 C 7.20E-03 C PM (filterable) 1.90E-03 C 4.30E-03 C

Criteria Pollutants and Greenhouse Gases Criteria Pollutants and Greenhouse Gases Nox 90-105% Load 3.17E+00 A Nox 90-105% Load 4.08E+00 B Pollutant Emission Factor Emission Factor Rating Pollutant Emission Factor Emission Factor Rating (lb/MMBtu) (lb/MMBtu) (fuel input) (fuel input)

CO <90% Load 3.53E-01 A CO <90% Load 5.57E-01 B CO 90 - 105% Load 3.86E-01 A CO 90 - 105% Load 3.17E-01 C Nox <90% Load 1.94E+00 A Nox <90% Load 8.47E-01 B

TOC 1.64E+00 A TOC 1.47E+00 A SO2 5.88E-04 A SO2 5.88E-04 A CO2 1.10E+02 A CO2 1.10E+02 A

PM10 (filterable) 3.84E-02 C PM10 (filterable) 7.71E-05 D VOC 1.20E-01 C VOC 1.18E-01 C Methane 1.45E+00 C Methane 1.25E+00 C

AP-42 Table 3.2-3. UNCONTROLLED EMISSIONS FACTORS FOR 4-STROKE RICH-BURN ENGINES (SCC 2-02-002-53)

Pollutant Emission Factor Emission Factor Rating (lb/MMBtu) (fuel input) PM Condensable 9.91E-03 E PM Condensable 9.91E-03 D PM2.5 (filterable) 3.84E-02 C PM2.5 (filterable) 7.71E-05 DAP-42 Table 3.3-1

* All particulate is assumed to be less than or equal to 1 micro meter in size.
AP-42 Table 3.4-1

0.00809 *S 1 1.01 *S 1 0.000406 *S 1 + 0.00957 *S 2 0.05 *S 1 + 0.895 *S 2

S 1 = % sulfur in fuel oil S 2= % sulfur in dual fuel
AP-42 Table 3.4-2
Pollutant CO2 1.10E+02 A SO2 5.88E-04 A CO 90 - 105% Load 3.72E+00 A CO <90% Load 3.51E+00 C Criteria Pollutants and Greenhouse Gases Nox 90-105% Load 2.21E+00 A Nox <90% Load 2.27E+00 C

PM2.5 (filterable) 9.50E-03 E PM Condensable 9.91E-03 E VOC 2.96E-02 C PM10 (filterable) 9.50E-03 E TOC 3.58E-01 C Methane 2.30E-01 C

PM-10 7.21E-04 0.1 2.20E-03 0.31 PM-2.5* 7.21E-04 0.1 2.20E-03 0.31 (lb/MMBtu) (lb/hp-hr) (lb/MMBtu) (Power output) (Fuel input) (Power output) (Fuel input) Pollutant Gasoline Fuel Diesel Fuel (SCC 2-02-003-01, 2-03-003-01) (SCC 2-02-001-02, 2-03-001-01) Emission Factor Emission Factor Emission Factor Emission Factor (lb/hp-hr)

CO 0.439 62.7 6.68E-03 0.95 TOC 0.021591 3.03 0.0025141 0.36 SO x 5.91E-04 0.084 2.05E-03 0.29 NO x 0.011 1.63 0.031 4.41

Crankcase 4.85E-03 0.69 4.41E-05 0.01

Refueling 1.08E-03 0.15 0 0

Exhaust 0.015 2.1 2.47E-03 0.35 Evaporative 6.61E-04 0.09 0 0

(lb/MMBtu) (lb/hp-hr) (lb/MMBtu) (Power output) (Fuel input) (Power output) (Fuel input) Pollutant Diesel Fuel Dual Fuel (SCC 2-02-004-01) (SCC 2-02-004-02) Emission Factor Emission Factor Emission Factor Emission Factor (lb/hp-hr)

Uncontrolled 0.024 3.2 0.018 2.7 Controlled 0.013 1.9 SO x NO x PM-10 0.0007 0.1 0 0 PM-2.5 0.0007 0.1 0 0

Nonmethane f f 1.32E-03 0.6 CO 5.50E-03 0.85 7.50E-03 1.16 TOC 7.05E-04 0.09 5.29E-03 0.8 Methane f f 3.97E-03 0.8

< 3 μm 0.0479 (lb/MMBtu) (fuel Input) Filterable particulate < 1 μm 0.04786 0.7

0.6 0.024

5 0.2
Storage Loading

AP-42 5.2 (eqn. (1)) SPM T L L= loading loss, pounds per 1000 gallons (lb/10^3 gal) of liquid loaded S = a saturation factor (see Table 5.2-1) 

### P = true vapor pressure of liquid loaded, pounds per square inch absolute (psia) M = molecular weight of vapors, pounds per pound-mole (lb/lb-mole) (see Table 7.1 T = temperature of bulk liquid loaded o R ( o F + 460) Condensable particulate 0.0077 Total PM-10 0.0573 Total particulate 0.0697 < 10 μm 0.0496 Total filterable particulate 0.062

Oil/water separators kg/10^3 L waste water Covered separators and/or vapor recovery systems lb/10^3 gal waste water Covered separators and/or vapor recovery systems See Chapter 7 - Liquid Storage Tanks Cooling towers kg/10^6 L cooling water 0.7 0.08 Minimization of bydrocarbon leaks into cooling water system; monitoring of cooling water for hydrocarbons lb/10^6 gal cooling water Minimization of bydrocarbon leaks into cooling water system; monitoring of cooling water for hydrocarbons AP-42 Table 5.1-2 (Metric And English Units). FUGITIVE EMISSION FACTORS FOR PETROLEUM REFINERIES
Emission

Source Emission Factor Units Emission Factor Applicable Control Technology ed Emissions Controlled Emissions

Submerged loading: dedicated normal service 0.60 Submerged loading: dedicated vapor balance service 1.00 Splash loading of a clean cargo tank 1.45 Cargo Carrier Mode Of Operation S Factor Tank trucks and rail tank cars Submerged loading of a clean cargo tank 0.50 See Section 5.2 - Transportation And Marketing Of Petroleum Liquids If cooling water rate is unknown (in liters or gallons) assume it is 40 times the refinery feed rate (in liters or gallons). Refinery feed rate is defined as the crude oil feed rate to the atmospheric distillation column. 1bbl (oil) = 42 gallons (gal), If waste water flow rate to oil/water separators is unknown (in liters or gallons) assume it is 0.95 times the refinery feed rate (in liters or gallons). Refinery feed rate is defined as the crude oil feed rate to the atmospheric distillation column. 1bb

L L= 12.46

AP-42 Table 5.2-1. SATURATION (S) FACTORS FOR CALCULATING PETROLEUM LIQUID LOADING LOSSES

Submerged loading: barges 0.50 Splash loading: dedicated normal service 1.45 Splash loading: dedicated vapor balance service 1.00 Marine vessels Submerged loading: ships 0.20AP-42 Table 11.6.4, Portland Cement Manufacturing PM (lbs/ton) 0.012
0.0031
0.019
0.032
0.0080 0.0024
0.0094
0.028
0.0010
0.00022
2.9E-05
0.00031

AP-42 Table 11.6.8, Portland Cement Manufacturing SO 2 NOx CO CO 2 TOC Wet Process Kiln 8.2 7.4 0.12 21000 0.028 (SCC 30500706) Long Dry Process Kiln 10 6.0 0.21 18000 0.028 (SCC 30500606) Preheater Process Kiln 0.55 4.8 0.98 18000 0.18 (SCC 30500622) Preheater/precalciner Kiln 1.1 4.2 3.7 18000 0.12 (SCC 30500623) Preheater/precalciner Kiln w/ Spray Tower 1.0 ND ND ND ND (SCC 30500623) AP-42 Table 11.9.1,Open Dust Sources at Western Surface Coal Mines
< 10 μm < 2.5 μm Units 0.000014 (A) 1.5 0.52 0.03 lb/blast 1.16 /(M) 1.2 0.119 /(M) 0.9 0.75 0.019 lb/ton Symbols for equations: A = horizontal area (ft2), with blasting depth # 70 ft. Not for vertical face of a bench. 78.4 (s) 1.2/(M) 1.3 18.6 (s) 1.5/(M) 1.4 0.75 0.022 lb/hr M = material moisture content (%)

5.7 (s) 1.2/(M) 1.3 1.0 (s) 1.5/(M) 1.4 0.75 0.105 lb/hr s = material silt content (%) u = wind speed (mph) 0.0021 (d) 1.1 / (M) 0.3 0.0021 (d) 0.7/ (M) 0.3 0.75 0.017 lb/yd 3 d = drop height (ft) W = mean vehicle weight (tons) S = mean vehicle speed (mph) Grading 0.040 (S) 2.5 0.051 (S) 2.0 0.60 0.031 lbs/VMT w = mean number of wheels (SCC 3-05-006-13) Raw mill feed belt with fabric filter (SCC 3-05-006-24) Raw mill weigh hopper with fabric filter (SCC 3-05-006-25) Raw mill air separator with fabric filter Process Raw mill with fabric filter

(SCC 3-05-006-11) Limestone transfer with fabric filter (SCC 3-05-006-12) Secondary limestone screening and crushing with fabric filter (SCC 3-05-006-10 + -11, 3-05-007-10 + -11)

Emission Factor Equation (SCC 3-05-006-28, 3-05-007-28) Finish grinding mill air separator with fabric filter (SCC 3-05-006-29, 3-05-007-29) Primary limestone crushing with fabric filter (SCC 3-05-006-09) Primary limestone screening with fabric filter (SCC 3-05-006-26) Finish grinding mill with fabric filter (SCC 3-05-006-17, 3-05-007-17) Finish grinding mill feed belt with fabric filter (SCC 3-05-006-27, 3-05-007-27) Finish grinding mill weigh hopper with fabric filter

Overburden Dragline Overburden Truck Loading Coal Bulldozing Coal Scaling Factors Operation Material TSP < 30 μm < 15 μm Blasting Coal or Overburden ND

Vehicle TrafficActive Storage Pile 0.72 U ND ND b/(acre-hr)

Table 11.9-4 UNCONTROLLED PARTICULATE EMISSION FACTORS FOR OPEN DUST SOURCES AT WESTERN SURFACE COAL MINES Mine TSP Material Location E F Units Overburden Any 1.3 lb/hole Coal V 0.22 lb/hole Topsoil Any 0.058 lb/ton IV 0.44 lb/ton Overburden Any 0.012 lb/ton Overburden V 0.037 lb/ton Coal Any 0.028 lb/ton III 0.0002 lb/ton Overburden V 0.002 lb/ton Coal IV 0.027 lb/ton III 0.005 lb/ton II 0.020 lb/ton I 0.014 lb/ton Any 0.066 lb/ton Coal V 0.007 lbs/ton Topsoil IV 0.04 lbs/ton Any 0.38 tons/acre-yr

AP-42 Table 11.12-2 Concrete Batching
Total PM Total PM10 Total PM Total PM 10 Aggregate transfer 0.0069 0.0033 ND ND (3-05-011-04, 21, 23) Sand Transfer 0.0021 0.00099 ND ND (3-05-011-05, 22, 24) 0.72 0.46 0.00099 0.00034 (3-05-011-07) 3.14 1.10 0.0089 0.0049 (3-05-011-17) Weigh hopper loading 0.0051 0.0024 ND ND (3-05-011-08) Mixer loading (central mix) 0.544 0.134 0.0173 0.0048 (3-05-011-09) Truck loading (truck mix) 0.995 0.278 0.0568 0.016 Drilling
Topsoil Removal by scraper Coal ND (Wind & Maintenance)

Source

End dump truck unloading (batch drop) Scraper unloading Bottom dump truck unloading (batch drop) Overburden Replacement
Truck loading by power shovel (batch drop) Train loading (batch or continuous drop)

Cement supplement unloading to elevated storage silo (pneumatic)

Wind erosion of exposed areas Seeding Land, stripping, overburden,

graded overburden

Emission factors are in lbs/ton Controlled Uncontrolled

Cement unloading to elevated storage silo (pneumatic)(3-05-011-10) AP-42 Table 11.17-6 (English Units). EMISSION FACTORS FOR LIME MANUFACTURING

ND ND 3.5 E 2.2 E ND NO X EMIS SION FACT

OR CO EMISSION FACTOR RATING CO 2 EMISSION FACTOR RATING Source SO 2 EMISSION FACTOR RATING SO 3 EMISSION FACTOR RATING

ND ND (SCC 3-05-016-18) Coal-fired rotary kiln with fabric filter 1.7 D ND ND C 1.5 D 3200 C (SCC 3-05-016-18) Coal-fired rotary kiln 5.4 D ND 3.1

Gas-fired rotary kiln (SCC 3-05-016-19) Coal-and gas fired rotary kiln with ND ND venturi scrubber (SCC 3-05-016-20) ND ND (SCC 3-05-016-18) Coal-fired rotary kiln with wet scrubber 0.3 D 0.21 E ND

ND 3000 D venturi scrubber (SCC 3-05-016-21) Coal-and coke-fired rotary kiln with ND ND ND 2.7 D 0.83 D 3200 D

6.3 E 2400 E multiclone, water spray, and fabric filter (SCC 3-05-016-22) Coal-fired rotary preheater kiln with
6.4 E ND ND ND ND PM controls (SCC 3-05-016-22) Coal-fired rotary preheater kiln with dry 2.3 E ND ND

D 0.45 D ND with fabric filter (SCC 3-05-016-23) Gas-fired parallel flow regenerative kiln 0.0012 D ND 0.24 D ND 2700 E (SCC 3-05-016-05) Gas-fired calcimatic kiln ND ND 0.15

Table 11.19.2-2 (English Units). EMISSION FACTORS FOR CRUSHED STONE PROCESSING OPERATIONS
Source Total PM EF Rating Total PM10 EF Rating Total PM-2.5 EF Rating ND 7.8 E (SCC 3-05-016-11) Product cooler ND ND ND

(SCC 3-05-020-02) Secondary Crushing (controlled) ND ND ND (SCC 3-05-020-02) Secondary Crushing ND ND ND (SCC 3-05-020-01) Primary Crushing (controlled) ND ND ND (SCC 3-05-020-01) Primary Crushing ND ND ND

(SCC 3-05-020-05) Fines Crushing (controlled) 0.003 E 0.0012 E 0.00007 E (SCC 3-05-020-05) Fines Crushing 0.039 E 0.015 E ND (SCC 3-05-030-03) Tertiary Crushing 0.0012 E 0.00054 C 0.0001 E (SCC 3-05-020-03) Tertiary Crushing 0.0054 E 0.0024 C ND

(SCC 3-05-020-21) Fines Screening (controlled) Fines Screening 0.3 E 0.072 E ND (SCC 3-05-020-02.03) Screening (controlled) 0.0022 E 0.0007 C 0.00005 E (SCC 3-05-020-02,03) Screening 0.025 E 0.0087 C NDAP-42 13.2.1 Paved Roads E = k(sL/2)^0.65 * (W/3)^1.5 - C (1) E ext= [k(sL/2)^0.65 (W/3)^1.5 - C] (1- P/4N) (2) E = Particulate emission factor (having units matching the units of k), k = Particle size multiplier for particle size range and units of interest sL = Road surface silt loading (grams per square meter)(g/m2) W = Average weight (tons) of the vehicles traveling the road, and 

### averaging period, and C = Emission factor for 1980's vehicle fleet exhaust, brake wear and tire wear. 

### monthly).
E ext= [k(sL/2)^0.65 (W/3)^1.5 - C] (1-1.2P/N) (3)



### averaging period, and N = Number of hours in the averagin period (e.g., 8760 for annual, 2124 for season 

### 720 for monthly).

g/VMT g/VKT lb/VMT 0.1617 0.1005 0.00036 0.2119 0.1317 0.00047 0.2119 0.1317 0.00047 0.2119 0.1317 0.00047

Range Mean Range Mean Units Range Mean 1 3 15.4 - 21.7 19 12.9-19.5 15.9 kg/km 188-400 292 45.8-69.2 55.4 lb/mi
9 48 1.1-35.7 12.5 .006-4.77 0.495 kg/km 0.09-79 9.7 0.0036 E 0.0022 E ND (SCC 3-05-020-21)

(SCC 3-05-020-10) Truck Unloading - Fragmented Stone ND 1.6E-05 E ND (SCC 3-05-020-31) Wet Drilling - Unfragmented Stone ND 8.0E-05 E ND (SCC 3-05-020-06) Conveyor Transfer Point (controlled) 0.00014 E 

### 4.6E-05 D 0.000013 E (SCC 3-05-020-06) Conveyor Transfer Point 0.003 E 0.0011 D ND

PM-2.5 0.66 1.1 0.0024 PM-10 4.6 7.3 0.016 P = Number of "wet"days with at least 0.254 mm (0.01 in) of precipitation during the

Table 13.2-1.1. PARTICLE SIZE MULTIPLIERS FOR PAVED ROAD EQUATION Size Range Particle Size Multiplier k g/VKT g/VMT lb/VMT (SCC 3-05-020-32)

E ext= Annual or other long-term average emission factor in the same units as k, P = Number of "wet"days with at least 0.254 mm (0.01 in) of precipitation during the N = Number of days in the averaging period (e.g., 365 for annual, 91 for seasonal, 30 for

E ext= Annual or other long-term average emission factor in the same units as k, Truck Unloading - Conveyor, crushed ND 0.00010 E ND

PM 30 Table 13.2.1-4 (Metric And English Units). TYPICAL SILT CONTENT AND LOADING VALUES FOR PAVED ROADS AT INDUSTRIAL FACILITIES Industry No. Of Sites No. Of Samples Silt Content (%) No. Of Travel Lanes Total Loading *10^-3 Stil Loading (g/m 2) Table 13.2.1-2. EMISSION FACTOR FOR 1980'S VEHICLE FLEET EXHAUST, BRAKE WEAR AND TIRE WEAR

Particle Size Range C, Emission Factor for Exhaust, Brake Wear and Tire Wear
PM 2.5 PM 10 PM 15 PM-15 5.5 9 0.02 PM-30 24 38 0.082

Copper Smelting 2

Iron and stell 2.020-16.9 1.75 lb/mi
1 3 2.6-4.6 3.3 12.1-18 14.9 kg/km 76-193 120 43.0-64.0 52.8 lb/mi 1 3 5.2-6.0 5.5 1.4-1.8 1.7 kg/km 11-12 12 5.0-6.4 5.9 lb/mi 1 3 6.4-7.9 7.1 2.8-5.5 3.8 kg/km 53-95 70 9.9-19.4 13.3 lb/mi
2 7 1.1-32.0 7.4

1 6 2.4-14 8.2 AP-42 13.2.2 Unpaved Roads

E = Size-specific emission factor (lb/VMT) s = Surface material Silt Content (%) PM-2.5 PM-10 PM-30 PM-2.5 PM-10 PM-30 W = Mean vehicle weight (tons) 0.15 1.5 4.9 0.18 1.8 6 M = Surface material moisture content (%) 0.9 0.9 0.7 1 1 1 S = Mean vehicle speed (mph) 0.45 0.45 0.45 C = Emission factor for 1980's vehicle fleet 0.2 0.2 0.3 exhaust, brake wear and tire wear 0.5 0.5 0.3 C B B C B B

E ext= Annual size-specific emission factor extrapolated for natural mitigation, lb/VMT E = Emission factor from Equation 1a and 1b P = Number of days in a year with at least 0.254 mm (0,01 in) of precipitation

AP-42 Table 13.2.4-3, Aggregate Handling And storage Piles (U / 5) 1.3 (M / 2) 1.4
EF = Emission factor in lbs/ton k = Partial Size Multiplier (Dimensionless) U = Mean Wind Speed in MPH M = Material Moisture Content (%) Aerodynamic Particle Size Multiplier (k) < 30 μm < 15 μm < 10 μm < 5 μm < 2.5 μm Quarry 2

E= k (s/12) a(W/3) b (1a) Industrial Sites
E = k (s/12) a(S/30) d - C (1b) Publicly Accessible Roads (M/0.5) c Concrete batching 2

Sand and gravel processing 1
Municipal solid

waste landfill 2

production Asphalt batching 1

Particle Size Range C, Emission Factor for Exhaust, Brake Wear and Tire Wear

lb/VMT PM 2.5 0.00036 PM 10 0.00047 b c d Quality Rating E ext= E [365 - P)/365] (2)

AP-42 Table 13.2.2-4. EMISSION FACTOR FOR 1980'S VEHICLE FLEET EXHAUST, BRAKE WEAR AND TIRE WEAR AP-42 Table 13.2.2-2 CONSTANTS FOR EQUATIONS 1a AND 1b
Constant Industrial Roads (Eq 1a) Public Roads (Eq 1b) k (lb/VMT) a

PM 30 0.00047

EF = k * 0.00320.74 0.48 0.35 0.2 0.053
Table 13.3-1 (Metric And English Units). EMISSION FACTORS FOR DETONATION OF EXPLOSIVES

Explosive Uses kg/Mg lbston kg/Mg lbston kg/Mg lbston Pollutant kg/Mg lbston 85 

### 170 ND ND 2.1 4.2 H 2 S 12 24 (38-120) 

### (72-240) (0.3-4.9) 0.6-9.7) (0-37) (0-73)
38 

### 77 ND ND 0.6 1.1 H 2 S 10 21 (34-42) 

### (68-84) (0.4-0.6) 0.7-1.5) (10-11) (20-21) Pb 0.6 1.2
141 

### 281 ND ND 1.3 2.5 H 2 S 3 6 (44-262) 

### (87-524) (0.3-2.8) 0.6-5.6) (0-7) (0-15)

32 

### 63 ND ND 0.7 1.3 H 2 S 16 31 (27-64) 

### (46-128) (0.3-1.1) 0.6-2.1) (9-19) (19-37)

52 

### 104 26 53 0.3 0.7 H 2 S 2 4 (13-110) 

### (26-220) (4-59) (8-119) (0.1-0.8) 0.3-1.7) (0-3) (0-6) SO 2 1 1 (0-8) (1-16) 34 

### 67 8 17 ND ND SO 2 1 2 (0-2) (1-3)

398 

### 796 ND ND 7.2 14.3 NH 3 14 29 (324-472) 

### (647-944) (6.6-7.7) 3.2-15.4) (14-15) (27-30) HCN 13 27 (11-16) (22-32) C 2 H 2 61 121 C 2 H 6 0.5 1.1
RDX (CH 2) 3 N 3 (NO 2) 3 98 

### 196 ND ND ND ND NH 3 22 44 (2.8-277) 

### (5.6-554) (12-61) (24-122)
PETN C(CH2ONO2)4 149 

### 297 ND ND ND ND NH 3 1.3 2.5 (138-160) 

### (276-319) (0-25) (0-5)

AP-42 Table 13.4-1 

### Particulate Emissions Factors for Wet Cooling Towers Smokeless Powder Nitrocellulose (sometimes with other materials) Small Arms propellant Dynamite Straight 20-60% Nitroglycorine/ sodium nitrate/woodpulp/ calcium carbonate Rarely Used Nitrogen Oxides Methane Other Composition Black Powder Potassium (sodium) nitrate/charcoal sulfur Delay Fuses Carbon Monoxide

BoosterCyclotrimethlynetrinitroamine Booster Penaerthritol tetranitrate

Tower Type Circulating ANFO Ammonium nitrate with 5.8-8% fuel oil Constructi on Work, Blasting in mines TNT Trinitrotoluene Main Charge in artillery projectiles, mortar rounds, etc. Dynamite Ammonia 20-60% Nitroglycorine/ sodium nitrate/woodpulp/ calcium carbonate Quarry Work Stump Blasting Dynamite gelatine 20-100% Nitroglycerine Demolishio n, Constructi on Work, blasting in

i



### Induced Draft 0.02 0.023 0.019 Natural Draft 0.00088 ND ND Water Flow PM10 PM10 (%) (g/daL) (lb/1000 gal)

### 0- 274 AP-42 Table II-7.1, Diesel Powered Mobile Sources

0.112 0.136 0.165 0.406 0.061 0.172 0.058 0.256 0.05 0.139 25.3 46.5 14.8 27.3 22.2 29.3 24 17.7 24.2 30.1
0.137 0.09 0.348 0.463 0.086 0.182 0.076 0.454 0.067 0.143 31.1 31.1 31.2 31.2 31.1 31.2 31.2 31.2 31.1 31.1
1.26 1.269 3.84 0.713 1.89 0.827 4.166 0.862 1.691 284.92 436.67 258.6 253.84 321.23 339.8 286.1 404.51 368.01
0.121 0.188 0.282 0.04 0.25 0.098 0.192 0.067 0.152 27.6 64.6 19 12.73 43.16 40.55 13.16 30.09 33.7
0.346 3.59 1.257 0.151 0.572 0.201 1.794 0.304 0.675 78.5 268.5 84.6 54.65 98.66 82.85 123.46 188.37 153.51 AP-42 Table II-7.2, Gasoline Powered Mobile Sources

0.024 0.0207 0.0298 0.026 0.0258 8.27 6.86 7 7.47 6.06
0.0155 0.0167 0.0234 0.0185 0.0234

5.2 5.31 5.31 5.28 5.28
0.43 0.32 0.518 0.362 0.412 146 102 121 100 95.8
0.362 0.41 0.531 0.611 0.56

122 132 124 176 130
0.0681 0.0661 0.0655 0.0622 0.056
0.0719 0.0818 0.106 0.122 0.112

9.52 12.1 15.6 13.4 17 3250 3910 3630 3840 3960



### Particulate SO2 NOx VOC CO 5.0 0.35 139.0 83.0 129.0 AP-42 Table 13.5-1 (English Units). EMISSION FACTORS FOR FLARE OPERATIONS EMISSION FACTOR RATING: B Component Emission Factor (lb/10 6Btu) Total hydrocarbons 

### 0.14

PM lb/hr lb/10 3 gal SOx lb/hr lb/10 3 gal Motor Grader Wheeled Loader Load er w/ Track OffHighwa y truck Roller Misc. Carbon monoxide 

### 0.37 Nitrogen oxides 

### 0.068 Soot

Pollutant Tractor w/ Track Wheeled Tractor Wheeled Dozer Scraper

Wheeled

loader Roller Misc. PM lb/hr lb/10 3 gal CO lb/hr lb/10 3 gal

Pollutant Wheeled Tractor Motor Grader NOx lb/hr lb/10 3 gal Exhaust Hydrocarbons lb/hr lb/10 3 gal

lb/hr CO lb/hr lb/10 3 gal EPA-450/4-90-003 Suggested Emission Factors for LPG Fuel (lbs/1000 gals burned) Exhaust Hydrocarbons lb/hr lb/10 3 gal Evaporative Hydrocarbons lb/hr Crankcase Hydrocarbons SOx lb/hr lb/10 3 gal NOx lb/hr lb/10 3 galEPA 453/R-95-017 Table 2-6 

### Refinery Screening Ranges Emission Factors Leaking Leaking No Leak No Leak VOC VOC VOC VOC (kg/hr/source) (lb/hr/source) (kg/hr/source) (lb/hr/source) 

### 0.263 0.579 0.00060 0.00132 0.085 0.188 0.00170 0.00375 0.000 0.001 0.00023 0.00051 0.437 0.963 0.01200 0.02646 0.389 0.856 0.01350 0.02976 1.608 3.545 0.08940 0.19709 1.691 3.728 0.04470 0.09855 0.038 0.083 0.00006 0.00013 0.012 0.026 0.00150 0.00331 EPA-453/R-95-017, Table 2-4 Oil and gas production operations average emission factors (kg/hr/source)



### 1.9E-05 Light Oil 2.5E-03 5.5E-03 Water / Oil 9.8E-05 2.2E-04 Equipment Type Service Emission Factor (kg/hr/source) Emission Factor (lbs/hr/source)
Valves Gas 4.5E-03 9.9E-03 Heavy Oil 8.4E-06

Light Oil 7.5E-03 1.7E-02 Water / Oil 1.4E-02 3.1E-02 Water / Oil 2.4E-05 5.3E-05 Others Gas 8.8E-03 1.9E-02 Heavy Oil 3.2E-05 7.1E-05 Pump Seals Gas 2.4E-03 5.3E-03 Heavy Oil NA NA Light Oil 1.3E-02 2.9E-02

Light Oil 1.1E-04 2.4E-04 Water / Oil 2.9E-06 6.4E-06 Water / Oil 1.1E-04 2.4E-04 Flanges Gas 3.9E-04 8.6E-04 Heavy Oil 3.9E-07 8.6E-07 Connectors Gas 2.0E-04 4.4E-04 Heavy Oil 7.5E-06 1.7E-05 Light Oil 2.1E-04 4.6E-04

Pump seals Light liquid Pump seals Heavy liquid Compressor seals Gas Valves Gas Valves Light liquid Valves Heavy liquid Water / Oil 2.5E-04 5.5E-04 Water / Oil emission factors apply to water streams in oil service with a water content greater than 50%, from the point of origin to the point where the water content reaches 99%. For water streams with a water content greater then 99%, the emissino rate is considered negligible. The "other" equipment type was derived from compressors, diaphrams, drains, dump arms, hatches, instruments, meters, pressure relief valves, polished rods, relief valves, and vents. This "other" equipment type should be applied for any equipment type other then connectors, flanges, open-ended lines, pumps, or valves.

Equipment Type Service 

### Open-ended lines Gas 2.0E-03 4.4E-03 Heavy Oil 1.4E-04 3.1E-04 Light Oil 1.4E-03 3.1E-03

Press. relief valves Gas Connectors All Open-ended lines AllEPA 453/R-95-017 Table 2-10 

### Refinery Screening Ranges Emission Factors

*SCR - Selective Catalytic Reduction **SNR - Selective Noncatalytic Reduction for Nox Valves/all 2.29E-06 0.746 Pump seals/all 

### 5.03E-05 0.610

Equipment Correlation Correlation Type/Service Constant Exponent

EPA AMMONIA FACTORS
EXTERNAL COMBUSTION BOILERS Electric Generation
FUEL TYPE OF BOILER CONTROL EMISSION FACTOR UNITS Flanges/all 

### 4.61E-06 0.703 Open-ended lines 2.20E-06 0.704 Others 1.36E-05 0.589 Connectors/all 

### 1.53E-06 0.735

0.630 lbs/ton UNCONTROLLED 0.000565 lbs/ton UNCONTROLLED 0.000565 lbs/ton Bituminous/Subbituminous Coal Pulverized Coal: Dry Bottom (Tangential) *SCR 0.310 lbs/ton (10100212) **SNR Bituminous/Subbituminous Coal Pulverized Coal: Wet Bottom *SCR 0.310 lbs/ton (10100201) **SNR 0.630 lbs/ton

18.000 lbs/10^6 cu ft UNCONTROLLED 3.200 lbs/10^6 cu ft UNCONTROLLED 0.800 lbs/10^3 gal Natural Gas Boilers > 100 Million Btu/hr except Tangential *SCR 9.100 lbs/10^6 cu ft (10100601) **SNR Distillage Oil Grades 1 and 2 Oil *SCR 1.400 lbs/10^3 gal (10100501) **SNR 2.900 lbs/10^3 gal

18.000 lbs/10^6 cu ft UNCONTROLLED 3.200 lbs/10^6 cu ft UNCONTROLLED 3.200 lbs/10^6 cu ft Natural Gas Tangentially Fired Units *SCR 9.100 lbs/10^6 cu ft (10100604) **SNR Natural Gas Boilers < 100 Million Btu/hr except Tangential *SCR 9.100 lbs/10^6 cu ft (10100602) **SNR 18.000 lbs/10^6 cu ft

Anthracite Coal Pulverized Coal *SCR 0.310 lbs/ton (10200102) **SNR 0.630 lbs/ton EXTERNAL COMBUSTION BOILERS Industrial
FUEL TYPE OF BOILER CONTROL EMISSION FACTOR UNITS



### Bituminous/Subbituminous Coal Pulverized Coal: Dry Bottom *SCR 0.310 lbs/ton (10200202) **SNR 0.630 lbs/ton 0.630 lbs/ton UNCONTROLLED 0.000565 lbs/ton UNCONTROLLED 0.000565 lbs/ton Bituminous/Subbituminous Coal Pulverized Coal: Wet Bottom *SCR 0.310 lbs/ton (10200201) **SNR

Bituminous/Subbituminous Coal Cogeneration *SCR 0.310 lbs/ton (10200219) **SNR 0.630 lbs/ton 0.630 lbs/ton UNCONTROLLED 0.000565 lbs/ton UNCONTROLLED 0.000565 lbs/ton Bituminous/Subbituminous Coal Spreader Stoker *SCR 0.310 lbs/ton (10200204) **SNR

### *SCR - Selective Catalytic Reduction **SNR - Selective Noncatalytic Reduction for Nox

*SCR - Selective Catalytic Reduction **SNR - Selective Noncatalytic Reduction for Nox

*SCR - Selective Catalytic Reduction **SNR - Selective Noncatalytic Reduction for Nox Residual Oil 10-100 Million Btu/hr *SCR 1.400 lbs/10^3 gal (10200402) **SNR 2.900 lbs/10^3 gal 2.900 lbs/10^3 gal UNCONTROLLED 0.800 lbs/10^3 gal UNCONTROLLED 0.000565 lbs/ton Residual Oil Grade 6 Oil *SCR 1.400 lbs/10^3 gal (10200401) **SNR

Natural Gas Boilers > 100 Million Btu/hr except Tangential *SCR 9.100 lbs/10^6 cu ft (10200601) **SNR 18.000 lbs/10^6 cu ft 2.900 lbs/10^3 gal UNCONTROLLED 0.800 lbs/10^3 gal UNCONTROLLED 0.800 lbs/10^3 gal Distillage Oil Grades 1 and 2 Oil *SCR 1.400 lbs/10^3 gal (10200501) **SNR

Natural Gas Tangentially Fired Units *SCR 9.100 lbs/10^6 cu ft (10200603) **SNR 18.000 lbs/10^6 cu ft 18.000 lbs/10^6 cu ft UNCONTROLLED 3.200 lbs/10^6 cu ft UNCONTROLLED 3.200 lbs/10^6 cu ft Natural Gas Boilers < 100 Million Btu/hr except Tangential *SCR 9.100 lbs/10^6 cu ft (10200602) **SNR

Bituminous/Subbituminous Coal Underfeed Stoker (Bituminous Coal) *SCR 0.310 lbs/ton (10300208) **SNR 0.630 lbs/ton UNCONTROLLED 3.200 lbs/10^6 cu ft

EXTERNAL COMBUSTION BOILERS Commercial/Industrial
FUEL TYPE OF BOILER CONTROL EMISSION FACTOR UNITS



### Distillage Oil < 10 Million Btu/hr *SCR 1.400 lbs/10^3 gal (10300503) **SNR 2.900 lbs/10^3 gal 2.900 lbs/10^3 gal UNCONTROLLED 0.800 lbs/10^3 gal UNCONTROLLED 0.000565 lbs/ton Distillage Oil Grades 1 and 2 Oil *SCR 1.400 lbs/10^3 gal (10300501) **SNR

EXTERNAL COMBUSTION BOILERS Space Heaters
TYPE OF BOILER FUEL CONTROL EMISSION FACTOR UNITS 

### 18.000 lbs/10^6 cu ft UNCONTROLLED 0.490 lbs/10^6 cu ft UNCONTROLLED 0.800 lbs/10^3 gal Natural Gas 10-100 Million Btu/hr *SCR 9.100 lbs/10^6 cu ft (10300602) **SNR

UNCONTROLLED 0.800 lbs/10^3 gal Industrial Natural Gas *SCR 9.100 lbs/10^6 cu ft (10500205) **SNR Industrial Distillate Oil *SCR 1.400 lbs/10^3 gal (10500105) **SNR 2.900 lbs/10^3 gal

(10500206) **SNR 18.000 lbs/10^6 cu ft

INTERNAL COMBUSTION ENGINES Electric Generation 

### lbs/10^3 gal UNCONTROLLED 0.800 lbs/10^3 gal Commercial/Institutional Natural Gas *SCR 9.100 lbs/10^6 cu ft 18.000 lbs/10^6 cu ft Commercial/Institutional Distillate Oil *SCR 1.400 lbs/10^3 gal (10500205) **SNR 2.900

### *SCR - Selective Catalytic Reduction **SNR - Selective Noncatalytic Reduction for Nox

*SCR - Selective Catalytic Reduction **SNR - Selective Noncatalytic Reduction for Nox

*SCR - Selective Catalytic Reduction **SNR - Selective Noncatalytic Reduction for Nox
PROCESS 

### (20100101) **SNR 2.900 lbs/10^3 gal Distillage Oil (Diesel) Reciprocating *SCR 1.400 lbs/10^3 gal (20100102) FUEL TYPE OF ENGINE CONTROL EMISSION FACTOR UNITS 

### Distillage Oil (Diesel) Turbine *SCR 1.400 lbs/10^3 gal

18.000 lbs/10^6 cu ft

INTERNAL COMBUSTION ENGINES Industrial
FUEL TYPE OF ENGINE CONTROL EMISSION FACTOR UNITS 

### **SNR 2.900 lbs/10^3 gal Natural Gas Reciprocating *SCR 9.100 lbs/10^6 cu ft (20100202) **SNR

Distillage Oil (Diesel) Reciprocating *SCR 1.400 lbs/10^3 gal (20200102) **SNR 2.900 lbs/10^3 gal Distillage Oil (Diesel) Turbine *SCR 1.400 lbs/10^3 gal (20200101) **SNR 2.900 lbs/10^3 gal

Distillage Oil (Diesel) Reciprocating: Exhaus *SCR 1.400 lbs/10^3 gal (20200107) **SNR 2.900 lbs/10^3 gal Distillage Oil (Diesel) Reciprocating: Cogeneration *SCR 1.400 lbs/10^3 gal (20200104) **SNR 2.900 lbs/10^3 gal

Natural Gas Reciprocating *SCR 9.100 lbs/10^6 cu ft (20200202) **SNR 18.000 lbs/10^6 cu ft Natural Gas Turbine *SCR 9.100 lbs/10^6 cu ft (20200201) **SNR 18.000 lbs/10^6 cu ft

Gasoline Reciprocating *SCR 1.400 lbs/10^3 gal (20200254) **SNR 2.900 lbs/10^3 gal Natural Gas 4-cycle Lean Burn *SCR 9.100 lbs/10^6 cu ft (20200254) **SNR 18.000 lbs/10^6 cu ft

Residual/Crude Oil Reciprocating *SCR 1.400 lbs/10^3 gal (20200501) **SNR 2.900 lbs/10^3 gal Large Bore Engine Diesel *SCR 1.400 lbs/10^3 gal (20200401) **SNR 2.900 lbs/10^3 gal

Distillage Oil (Diesel) Reciprocating *SCR 1.400 lbs/10^3 gal (20300101) **SNR 2.900 lbs/10^3 gal INTERNAL COMBUSTION ENGINES Industrial
FUEL TYPE OF ENGINE CONTROL EMISSION FACTOR UNITS 

### Kerosene/Naphtha (Jet Fuel) Reciprocating *SCR 1.400 lbs/10^3 gal (20200902) **SNR 2.900 lbs/10^3 gal

Gasoline Reciprocating *SCR 1.400 lbs/10^3 gal (20300301) **SNR 2.900 lbs/10^3 gal Natural Gas Turbine *SCR 9.100 lbs/10^6 cu ft (20300202) **SNR 18.000 lbs/10^6 cu ft

Chemical Manufacturing Prilling Tower: Low Density Ammonia Production (20100308) Chemical Manufacturing Prilling Tower: High Density UNCONTROLLED 57.200 lbs/ton Ammonium Nitrate Production (30102712) INDUSTRIAL PROCESSES
TYPE OF OPERATION CONTROL EMISSION FACTOR UNITS 

### Chemical Manufacturing Carbon Dioxide Regenerator UNCONTROLLED 2.000 lbs/ton

### g y UNCONTROLLED 0.260 lbs/ton Ammonium Nitrate Production

Chemical Manufacturing Evaporation/concentration operation UNCONTROLLED 0.54- 33.400 lbs/ton Ammonium Nitrate Production Chemical Manufacturing Neutralizer UNCONTROLLED .86 - 36.020 lbs/ton Ammonium Nitrate Production Chemical Manufacturing Prilling Tower: Low Density UNCONTROLLED 0 - 3.180 lbs/ton Ammonium Nitrate Production (30102725)

Chemical Manufacturing Prilling Cooler: Low Density UNCONTROLLED 0.300 lbs/ton Ammonium Nitrate Production Chemical Manufacturing Prilling Cooler: High Density UNCONTROLLED 0.040 lbs/ton Ammonium Nitrate Production Chemical Manufacturing Rotary drum granulators UNCONTROLLED 59.400 lbs/ton Ammonium Nitrate Production

Primary Metal Production Oven Charging UNCONTROLLED 0.020 lbs/ton By-product Coke Manufacturing (30300302) Food and Agricultural Industries Blood Dryers CONTROL 0.600 lbs/ton Meat Rendering Plants Chemical Manufacturing Plant emissions CONTROL 0.080 lbs/ton Ammonium Phosphate

Mineral Production Kilns FABRIC FILTER 0.010 lbs/ton Cement Manufacturing (Dry Process) (30500606) Primary Metal Production Oven/Door Leaks UNCONTROLLED 0.060 lbs/ton By-product Coke Manufacturing (30300308 Primary Metal Production Oven Pushing UNCONTROLLED 0.100 lbs/ton By-product Coke Manufacturing (30300303)

Mineral Products Kilns FABRIC FILTER 0.010 lbs/ton Cement Manufacturing (Dry Process) (30500623) Mineral Products Kilns FABRIC FILTER 0.010 lbs/ton Cement Manufacturing (Dry Process) (30500622) Mineral Products Kilns FABRIC FILTER 0.010 lbs/ton Cement Manufacturing (Dry Process) (30500706)

Mineral Products Preheater/Precalciner kiln FABRIC FILTER 0.010 lbs/ton Cement Manufacturing (Dry Process) (30500706) Mineral Products Preheater/Precalciner kiln FABRIC FILTER 0.010 lbs/ton Cement Manufacturing (Dry Process) (30500606) Mineral Products Preheater/Precalciner kiln FABRIC FILTER 0.010 lbs/ton Cement Manufacturing (Dry Process) (30500623)

Mineral Products Kilns FABRIC FILTER 0.010 lbs/ton Cement Manufacturing (Dry Process) (30500706) Mineral Products Kilns FABRIC FILTER 0.010 lbs/ton Cement Manufacturing (Dry Process) (30500606) Mineral Products Preheater/Precalciner kiln FABRIC FILTER 0.010 lbs/ton Cement Manufacturing (Dry Process) (30500622)

Mineral Products Preheater Kiln FABRIC FILTER 0.010 lbs/ton Cement Manufacturing (Dry Process) (30500622) Mineral Products Kilns FABRIC FILTER 0.010 lbs/ton Cement Manufacturing (Dry Process) (30500623) Mineral Products Kilns FABRIC FILTER 0.010 lbs/ton Cement Manufacturing (Dry Process) (30500622)

Mineral Products Preheater Kiln FABRIC FILTER 0.010 lbs/ton Cement Manufacturing (Dry Process) (30500623) Mineral Products Preheater Kiln FABRIC FILTER 0.010 lbs/ton Cement Manufacturing (Dry Process) (30500706) Mineral Products Preheater Kiln FABRIC FILTER 0.010 lbs/ton Cement Manufacturing (Dry Process) (30500606)

Petroleum Industry Moving-/Bed Catalytic Cracking Unit UNCONTROLLED 6.000 lbs/ton Catalytic Cracking Units Petroleum Industry Fluid Catalytic Cracking Unit UNCONTROLLED 54.000 lbs/ton Catalytic Cracking Units (30600201)

### *SCR - Selective Catalytic Reduction **SNR - Selective Noncatalytic Reduction for Nox Petroleum Industry Plant Gas UNCONTROLLED 200.000 lbs/ton Compressor Engines