FORM A-1

PARENT COMPANY INFORMATION

I. Parent Company / Legal Corporate Owner Information

 1. Legal Parent Company / Legal Corporate Name Industrial Insulation Group LLC

 2. Address 2100 Line Dr

 3. City Brunswick

 4. State GA

 5. Zip Code

 6. County

 7. Size of Company (approximate number of employees including all 

subsidiaries, branches, and related establishments owned): 425
FORM A-2

FACILITY INFORMATION

II. Facility Information

 Facility Name IIG Minwool

 Facility Address

 Street 908 John Bussey Dr

 City Phenxi City

 State AL

 Zip Code 36869

 County Russell

 Facility Coordinates

 Latitude (decimal degrees, six decimal places) 32.36179173

 Longitude (decimal degrees, six decimal places) -91.57582171

 Specific location represented (e.g., front door of main building, 

centroid of property, etc.) As listed in Title V documentation

 Number of employees attached to the mineral wool production 

facility: CBI

 Design capacity of the plant (tons/yr) CBI

 Type(s) of process(es) (rotary spin, flame attenuation) at this plant Cupola, rotary spins, curing oven

 Operation schedule

 hrs/day 24

 days/yr approximately 244

 Identify what state and local air pollution rules and regulations, 

including permit requirements, your plant is subject to. (Please 

provide copies of permit(s) and permit IDs) Title V Alabama see attached permit

III. Technical Contact

Original Contact:

 Name Jessie Payne

 Technical Contact Title Corporate EHS Manager

 Telephone 281-605-4630 or 334-507-9386-Cell

 Facsimile (Fax) 334-298-5429
 Email paynej@iig-llc.com

IV. Other

 Is the facility a major source of HAP? Yes

 

 If "No", did the facility take a limit of its potential HAP emissions 

to avoid classification as a major source? NA

 Does the facility manufacture other products in addition to 

mineral wool? No

 If "Yes", list the other products manufactured at the facility. NA

 Are there any HAP emissions associated with any co-located 

facilities? List unit operations, e.g., boiler, and pollutant/emissions NO
FORM A-2

FACILITY INFORMATION

II. Facility Information

 Facility Name

 Facility Address

 Street

 City

 State

 Zip Code

 County

 Facility Coordinates

 Latitude (decimal degrees, six decimal places)

 Longitude (decimal degrees, six decimal places)

 Specific location represented (e.g., front door of main building, 

centroid of property, etc.)

 Number of employees attached to the mineral wool production 

facility:

 Design capacity of the plant (tons/yr)

 Type(s) of process(es) (rotary spin, flame attenuation) at this plant

 Operation schedule

 hrs/day

 days/yr

 Identify what state and local air pollution rules and regulations, 

including permit requirements, your plant is subject to. (Please 

provide copies of permit(s) and permit IDs)

III. Technical Contact

 Name

 Technical Contact Title

 Telephone

 Facsimile (Fax)

Interim Replacement:

Rick Dolin

Chief Product Analyst

970-858-9458

970-858-9641
 Email

IV. Other

 Is the facility a major source of HAP?

 

 If "No", did the facility take a limit of its potential HAP emissions 

to avoid classification as a major source?

 Does the facility manufacture other products in addition to 

mineral wool?

 If "Yes", list the other products manufactured at the facility.

 Are there any HAP emissions associated with any co-located 

facilities? List unit operations, e.g., boiler, and pollutant/emissions

dolinr@iig-llc.com
FORM B-1

PLANT OPERATIONS

I. Overview of Process Operations

Number of process lines. Include lines that are currently

operational or that are temporarily shutdown. (Do not 

include lines permanently shutdown). 2

For each process line: Process Line 1 Process Line 2 Process Line 3

Process line identification name or numbers Board Pipe

Type of process line (e.g., Fiberization method) Fiberization Fiberrization

Maximum annual production rate (tons/yr)

Age of process line (yrs) 20 yr 20 yr

Remaining economic life of process line (yrs)

Indefinite with ongoing 

maintenance program.

Indefinite with ongoing 

maintenance program.

List of products produced and most recent annual 

production (tons/yr; specify year) for each product Mineral Wool Mineral Wool

Please attach detailed schematics of each process line NA-
FORM B-2

PROCESS OPERATIONS

II. Raw Material Handling and Storage

 Cupola charge preparation

 Raw materials and proportions by wt (%) CBI

 Method(s) of conveying each raw material to cupola Conveyor

 Binder and Additives

 List each raw material, including premixed materials, in 

the binder formulation and its proportion by wt (%) CBI

 List steps in preparing binder, including storage 

temperature (°F) and holding time (hrs) CBI

 Total yearly consumption of binder, excluding water, 

(gal/yr) CBI

 Cost of binder, excluding water, ($/gal) for most recent 

year (specify year) CBI

 Are binder storage and mixing tanks vented to 

outside/inside? Inside

 Method of treating vent air from storage and mix tanks None

 Emission control during liquid raw material transfer from 

vehicles to storage tanks. Closed system

 Describe future source reduction plans and schedules to 

reformulate binders; List each constituent, proportions wt 

(%), cost ($/gal) for reformulation None at this time
FORM B-3

PROCESS OPERATIONS

III. Cupola/furnace

 For each cupola: Cupola 1 Cupola 2 Cupola 3

 Process unit identification name/number 1

 Process line(s) served (identification name/number) 2

 Latitude (decimal degrees, six decimal places) 32.430118

 Longitude (decimal degrees, six decimal places) -84.978139

 Stack or vent height (units) Stack 200 ft

 Stack or vent diameter (units) Stack 8 ft Dia.

 Manufacturer and model Jungers Verstad AB

 Date of original installation 1988-1989

 Estimate of remaining lifetime (yrs)

 Major rebuilds:

 What constitutes a major rebuild

 Frequency of a major rebuild NA

 Cost of typical major rebuild NA

 Date of last major rebuild NA

 Purpose of last major rebuild NA

 Increase or decrease in emissions NA

 Fuel type: coke, electric, gas, or oil NA

Mod or change of ops that affects permiting requirements

Continued maintenance can maintain indefinite life,

 Fuel consumption rate (KW/ton of melt or Btu/ton of melt) NA

 Design production rate (tons/day) NA

 Actual glass pull rate (tons/day) NA

 Exhaust air flow rate (acfm @ °F) NA

 Temperature (°F) of melt as it exits the cupola NA

 Is oxygen enrichment used to supplement combustion air NA

 Quantity of oxygen supplied for enrichment (cu. Ft. O2/ton 

coke) NA

 Nature and frequency of routine/preventive maintenance 

procedures NA

 Describe process modification(s) since 1999 that reduce 

emissions None

 Describe future source reduction plans and schedules
FORM B-4

PROCESS OPERATIONS

IV. Fiberization

 For each fiberization operation: Fiberization Operation 1 Fiberization Operation 2 Fiberization Operation 3

 Process unit identification name/number

 Process line(s) served (identification name/number) Board/Pipe

 Latitude (decimal degrees, six decimal places) 32.430149

 Longitude (decimal degrees, six decimal places) -84.978027

 Stack or vent height (units) Stack 200 feet

 Stack or vent diameter (units) Stack Dia 8.5 feet

 Number of fiber forming devices (spinners) per line 2

 Method of attenuation fiber (air, centrifical force, or both) Both

 Major rebuilds:

What constitutes a major rebuild

 Frequency of a major rebuild NA

 Cost of typical major rebuild NA

 Date of last major rebuild NA

 Purpose of last major rebuild NA

 Increase or decrease in emissions NA

 If forming section is modular, i.e., more than one forming 

and collection area per line, indicate the number of modules and 

air plenums. NA

 Presence of water overspray and application range (gpm) NA

 Binder applied and application rate (gpm) CBI

 Other material applied (annealing oil or oil/water emulsion) 

and application rate (gpm) CBI

 Temperature of binder when applied to the fibers (°F) CBI

 Forming air flow rate (acfm @ °F) CBI

 Percent of forming air recirculated and percent exhausted CBI

 Nature and frequency of routine/preventive maintenance 

procedures

Based on SSM/OMM Plan 

attached.

 Describe process modification(s) since 1999 that reduce 

emissions None

 Describe future source reduction plans and schedules

Mod or change of ops that affects permiting requirements
 Fiberization method (e.g., Downey process or Youger/Powell 

process)

 Number of rotors

 Configuration of rotor(s)

 Amount of material that remains non-fiberized shot

 Exhaust air flow rate (acfm @ °F)
FORM B-5

PROCESS OPERATIONS

V. Fiber Collection

 For each fiber collection operation: Fiber Collection Operation 1 Fiber Collection Operation 2 Fiber Collection Operation 3

 Process unit identification name/number 1

 Process line(s) served (identification name/number) Board/Pipe

 Latitude (decimal degrees, six decimal places) 32.430149

 Longitude (decimal degrees, six decimal places) -84.97812

 Stack or vent height (units) Stack 200 feet

 Stack or vent diameter (units) Stack Dia 8.5 feet

 Method of fiber collection from fiberization Rotating Drum

 Manufacturer and model of collection chamber

 Date of original installation

 Major rebuilds:

 What constitutes a major rebuild

 Frequency of a major rebuild NA

 Cost of typical major rebuild NA

 Date of last major rebuild NA

 Purpose of last major rebuild NA

 Increase or decrease in emissions NA

 Air flow rate (acfm @ °F) in pneumatic fiber conveying CBI

 Exhaust air flow rate (acfm @ °F)

 Residence time of product (mins) (time spent in 

collection device) CBI

 Method of evenly distributing fibers onto conveyor belt

 Formed mat thickness (in.) Varies 

 Nature and frequency of routine/preventive 

maintenance procedures Monthly/Annually PM

 Describe process modification(s) since 1999 that 

reduce emissions None

 Describe future source reduction plans and schedules

Mod or change of ops that affects permiting requirements
FORM B-6

PROCESS OPERATIONS

VI. Curing 

 For each curing oven: Curing Oven 1 Curing Oven 2 Curing Oven 3

 Process unit identification name/number 1

 Process line(s) served (identification name/number) Board/Pipe

 Latitude (decimal degrees, six decimal places) 32.430246

 Longitude (decimal degrees, six decimal places) -84.97802

 Stack or vent height (units) Stack 200 feet

 Stack or vent diameter (units) Stack Dia 8.5 feet

 Method of curing Gas Heat

 Manufacturer and model Jungers Verstad AB

 Date of original installation

 Major rebuilds:

 What constitutes a major rebuild

 Frequency of a major rebuild NA

 Cost of typical major rebuild NA

 Date of last major rebuild NA

 Purpose of last major rebuild NA

 Increase or decrease in emissions NA

 Fuel type: electric, gas, or oil Gas Heat

 Fuel consumption rate (KW/hr or BTU/hr)

 Curing temperature (°F) 354

 Moisture content wt (%) of formed mat: 

 inlet 4.8

 outlet 4.8

 Exhaust air flow rate (acfm @ °F) from curing

 Residence time of product (mins) Variable

 Binder content of cured product (LOI)

 Nature and frequency of routine/preventive maintenance 

procedures See attached OMM/SSM

 Describe process modification(s) since 1999 that reduce 

emissions None

 Describe future source reduction plans and schedules None

Mod or change of ops that affects permiting requirements
FORM B-7

PROCESS OPERATIONS

VII. Cooling

 For each cooling operation: Cooling Operation 1 Cooling Operation 2 Cooling Operation 3

 Process unit identification name/number 1

 Process line(s) served (identification name/number) Board

 Latitude (decimal degrees, six decimal places) 32.430753

 Longitude (decimal degrees, six decimal places) -84.978309

 Stack or vent height (units) NA

 Stack or vent diameter (units) NA

 Cooling air flow rate (acfm @ °F) NA

 Percentage of cooling air recirculated (if any) NONE

 Cooling air temperature (°F) NA

 Exhaust air flow rate (acfm @ °F) NA

 Nature and frequency of routine/preventive maintenance 

procedures Monthly/Annually

 Describe process modification(s) since 1999 that reduce 

emissions NONE

 Describe future source reduction plans and schedules
FORM B-8

PROCESS OPERATIONS

VIII. Pollution Prevention

Please describe any work practices, pollution prevention techniques, 

and control strategies evaluated and/or implemented at each process 

unit at your facility (e.g., binder reformulation, alternative fuels usage, 

etc.) to reduce emissions of PM, CO, and HAPs you identified in Form 

E. You must specify the year in which the facility implemented the 

practice/technique and identify the emission reductions (if measured) 

from these practices/techniques. NONE
FORM C-1

AIR POLLUTION CONTROL

I. Electrostatic Precipitator (ESP) (none)

 For each ESP: ESP 1 ESP 2 ESP 3

 Process line(s) (identification name/number)

 Equipment/process(es) controlled. Include emission point 

designations (e.g., E3, E4 from plot plan)

 Latitude (decimal degrees, six decimal places)

 Longitude (decimal degrees, six decimal places)

 Stack or vent height (units)

 Stack or vent diameter (units)

 Manufacturer and model

 Date of original installation

 Number of collection plates and configuration

 Gas flow rate to ESP (acfm @ °F)

 Inlet gas temperature (°F)

 Outlet gas temperature (°F)

 Inlet grain loading (gr/dscf)

 Outlet grain loading (gr/dscf)

 Average stack opacity (%)

 Pressure drop across ESP (in. H

2O gauge)

 Plate area (ft

2

)

 Vendor guarantee on ESP efficiency (attach copy)

 Method of plate cleaning and frequency

 Flow rate of plate wash water to ESP (gpm), if applicable

 Temperature of plate wash water to ESP (°F), if applicable

 Source of plate wash water used for cleaning, if applicable

 Concentration (mg/l) of dissolved and suspended solids in plate 

wash water, if applicable

 Conditioning agents used and amounts (in gpm or lbs/hr), if 

applicable

 Amount of wastewater generated (gpd), if applicable

 Amount of wastewater recycled (gpd), if applicable

 Amount of wastewater disposed of (gpd), if applicable

 Method of wastewater disposal, if applicable

 Quantity of solid waste collected (lbs/yr)

 Quantity of solid waste recycled (lbs/yr)

 Quantity of solid waste disposed of (lbs/yr)
 Method of solid waste disposal

 Nature and frequency of routine/preventive maintenance 

procedures

 Problems experienced with control device within the last five 

years; how were problems solved?

 Continuous monitoring method(s) used to monitor ESP 

performance, including parameters monitored

 Describe any plans to replace or upgrade ESP
FORM C-2

AIR POLLUTION CONTROL

II. Scrubber (none)

 For each scrubber: Scrubber 1 Scrubber 2 Scrubber 3

 Process line(s) (identification name/number)

 Equipment/process(es) controlled. Include emission point 

designations (e.g., E3, E4 from plot plan)

 Latitude (decimal degrees, six decimal places)

 Longitude (decimal degrees, six decimal places)

 Stack or vent height (units)

 Stack or vent diameter (units)

 Manufacturer and model

 Date of original installation

 Type (e.g., venturi, orifice)

 Gas flow rate to scrubber (acfm @ °F)

 Inlet gas temperature (°F)

 Outlet gas temperature (°F)

 Inlet grain loading (gr/dscf)

 Outlet grain loading (gr/dscf)

 Average stack opacity (%)

 Water flow rate to scrubber (gpm)

 Percent of scrubber water from recycled wastewater

 Source of scrubbing water and type of pretreatment. Substance(s) 

added as part of pretreatment and amount used (gpm or lbs/hr)

 HAP composition of wastewater (mg/L)

 Concentration (mg/L) of dissolved and suspended solids in 

scrubbing water

 Scrubbing water temperature (°F)

 Liquid/gas ratio (gal/103 acfm)

 Pressure drop across scrubber (in. H2O gauge)

 Amount of wastewater generated (gpd)

 Amount of wastewater recycled (gpd)

 Amount of wastewater disposed of (gpd)
 Method of wastewater disposal

 Quantity of solid waste collected (lbs/yr)

 Quantity of solid waste recycled (lbs/yr)

 Quantity of solid waste disposed of (lbs/yr)

 Method of solid waste disposal

 Vendor guarantee on scrubber efficiency (attach copy)

 Nature and frequency of preventive maintenance procedures

 Problems experienced with control device within the last five years; 

how were problems solved?

 Continuous monitoring method(s) used to monitor scrubber 

performance, including parameters monitored

 Plans to replace or upgrade scrubber
FORM C-3

AIR POLLUTION CONTROL

III. Mechanical Collector (none)

 For each mechanical collector: Mechanical Collector 1 Mechanical Collector 2 Mechanical Collector 3

 Process line(s) (identification name/number)

 Equipment/process(es) controlled. Include emission point 

designations (e.g., E3, E4 from plot plan)

 Latitude (decimal degrees, six decimal places)

 Longitude (decimal degrees, six decimal places)

 Stack or vent height (units)

 Stack or vent diameter (units)

 Manufacturer and model

 Date of original installation

 Type of mechanical collector 

 Gas flow rate to collector (acfm @ °F)

 Inlet gas temperature (°F)

 Outlet gas temperature (°F)

 Inlet grain loading (gr/dscf)

 Outlet grain loading (gr/dscf)

 Average stack opacity (%)

 Overall pressure drop (in. H2O gauge)

 Vendor guarantee on mechanical collector efficiency (attach 

copy)

 Quantity of solid waste collected (lbs/yr)

 Quantity of solid waste recycled (lbs/yr)

 Quantity of solid waste disposed of (lbs/yr)

 Method of solid waste disposal

 Nature and frequency of preventive maintenance procedures

 Problems experienced with control device within the last five 

years; how were problems solved?

 Continuous monitoring method(s) used to monitor performance, 

including parameters monitored

 Plans to replace or upgrade mechanical collector
FORM C-4

AIR POLLUTION CONTROL

IV. Fabric Filter 

 For each fabric filter: Fabric Filter 1 Fabric Filter 2 Fabric Filter 3

 Process line(s) (identification name/number) Board 

 Equipment/process(es) controlled. Include emission point 

designations (e.g., E3, E4 from plot plan) Curing Oven

 Latitude (decimal degrees, six decimal places)

 Longitude (decimal degrees, six decimal places)

 Stack or vent height (units) 200 ft

 Manufacturer and model Custom Built 

 Date of original installation 1989

 Number of compartments

 Number of bags per compartment 315

 Filter material and coatings applied

See attached Filtration 

Fabric Datasheet

 Fabric weight (oz/yd

2

) 14

 Filter surface area (ft2)

 Gas flow rate to filter (acfm @ °F)

 Inlet gas temperature (°F)

 Outlet gas temperature (°F)

 Inlet grain loading (gr/dscf)

 Outlet grain loading (gr/dscf)

 Average stack opacity (%) <1 

 Overall pressure drop (in. H2O gauge)

 Method and frequency of bag cleaning

 Vendor guarantee on fabric filter efficiency (attach copy)

 Quantity of solid waste collected (lbs/yr)

 Quantity of solid waste recycled (lbs/yr)

 Quantity of solid waste disposed of (lbs/yr)

 Method of solid waste disposal
 Nature and frequency of preventive maintenance 

procedures See OMM/SSM

 Problems experienced with control device within the last five 

years; how were problems solved? None

 Continuous monitoring method(s) used to monitor 

performance, including parameters monitored Pressure/Temp

 Plans to replace or upgrade fabric filter No 
FORM C-5

AIR POLLUTION CONTROL

V. Thermal Incinerator

 For each thermal incinerator Thermal Incinerator 1 Thermal Incinerator 2 Thermal Incinerator 3

 Process line(s) (identification name/number) Envirotech NONE NONE

 Equipment/process(es) controlled. Include emission point 

designations (e.g., E3, E4 from plot plan)

Controls Cupola, Fiber 

collection, emission point 

stack # 1. NONE NONE

 Latitude (decimal degrees, six decimal places) 32.42989 NONE NONE

 Longitude (decimal degrees, six decimal places) -84.978132 NONE NONE

 Stack or vent height (units) 200 NONE NONE

 Stack or vent diameter (units) 8.5 feet NONE NONE

 Manufacturer and model Envirotech NONE NONE

 Date of original installation 1989 NONE NONE

 Fuel type: gas or oil Natural Gas NONE NONE

 Fuel consumption rate (BTU/hr) NONE NONE

 Inlet gas flow rate (acfm @ °F) 7080 NONE NONE

 Inlet gas temperature (°F) 376 NONE NONE

 Combustion chamber gas temperature (°F) 1500 NONE NONE

 Outlet gas temperature (°F) 586 NONE NONE

 Inlet grain loading (gr/dscf) NONE NONE

 Outlet grain loading (gr/dscf) NONE NONE

 Average stack opacity (%) Less than 1% NONE NONE

 Excess air (%) NONE NONE

 Residence time (sec) at temperature (°F) 1 sec @ 1500 NONE NONE

 Percent heat recovery NONE NONE

 Vendor guarantee on incinerator efficiency (attach copy) Unavailable NONE NONE

 Nature and frequency of preventive maintenance procedures See attached MACT/SSM NONE NONE

 Problems experienced with control device within the last five 

years; how were problems solved? NONE NONE NONE

 Continuous monitoring method(s) used to monitor incinerator 

performance, including parameters monitored NONE NONE
 Plans to replace or upgrade thermal incinerator None NONE NONE
FORM C-6

AIR POLLUTION CONTROL

VI. High Velocity Air Filter (HVAF) (none)

 For each HVAF: HVAF 1 HVAF 2 HVAF 3

 Process line(s) (identification name/number)

 Equipment/process(es) controlled. Include emission 

point designations (e.g., E3, E4 from plot plan)

 Latitude (decimal degrees, six decimal places)

 Longitude (decimal degrees, six decimal places)

 Stack or vent height (units)

 Stack or vent diameter (units)

 Manufacturer and model

 Date of original installation

 Inlet gas flow rate (acfm @ °F)

 Inlet gas temperature (°F)

 Outlet gas temperature (°F)

 Inlet grain loading (gr/dscf)

 Outlet grain loading (gr/dscf)

 Average stack opacity (%)

 Water spray pressure (psig), if applicable

 Water spray rate (gpm), if applicable

 Filter face velocity (acfm/ft2)

 Maximum pressure drop across mat (in. H2O gauge)

 Vendor guarantee on HVAF efficiency (attach copy)

 Method and frequency of filter mad advancement

 Amount of wastewater generated (gpd)

 Amount of wastewater recycled (gpd)

 Amount of wastewater disposed of (gpd)

 Method of wastewater disposal

 Quantity of solid waste collected (lbs/yr)

 Quantity of solid waste recycled (lbs/yr)

 Quantity of solid waste disposed of (lbs/yr)

 Method of solid waste disposal
 Nature and frequency of preventive maintenance 

procedures

 Problems experienced with control device within the last 

five years; how were problems solved?

 Continuous monitoring method(s) used to monitor 

HVAF performance, including parameters monitored

 Plans to replace or upgrade HVAF
FORM C-7

AIR POLLUTION CONTROL

VII. Mist Eliminator (none)

 For each mist eliminator: Mist Eliminator 1 Mist Eliminator 2 Mist Eliminator 3

 Process line(s) (identification name/number)

 Equipment/process(es) controlled. Include emission point 

designations (e.g., E3, E4 from plot plan)

 Latitude (decimal degrees, six decimal places)

 Longitude (decimal degrees, six decimal places)

 Stack or vent height (units)

 Stack or vent diameter (units)

 Manufacturer and model

 Date of original installation

 Type of mist eliminator

 Gas flow rate to mist eliminator (acfm @ °F)

 Inlet gas temperature (°F)

 Outlet gas temperature (°F)

 Inlet grain loading (gr/dscf)

 Outlet grain loading (gr/dscf)

 Average stack opacity (%)

 Velocity in mist eliminator (ft/sec)

 Pressure drop (in. H2O gauge)

 For chevron blade mist eliminators:

 Spacing between blades (in.)

 Washing frequency of blades

 For mesh pad mist eliminators:

 Number of pads or elements

 Thickness of pad (in.) or element dimensions

 Density of pad, (lb/ft3)

 Washing frequency of pad

 Vendor guarantee on mist eliminator efficiency (attach copy)

 Amount of wastewater generated (gpd)

 Amount of wastewater recycled (gpd)
 Amount of wastewater disposed of (gpd)

 Method of wastewater disposal

 Quantity of solid waste collected (lbs/yr)

 Quantity of solid waste recycled (lbs/yr)

 Quantity of solid waste disposed of (lbs/yr)

 Method of solid waste disposal

 Nature and frequency of preventive maintenance procedures

 Problems experienced with control device within the last five 

years; how were problems solved?

 Continuous monitoring method(s) used to monitor mist eliminator 

performance, including parameters monitored

 Plans to replace or upgrade mist eliminator 
FORM C-8

AIR POLLUTION CONTROL

VIII. Ventilation System (none)

 For each ventilation system: Ventilation System 1 Ventilation System 2 Ventilation System 3

 Process line(s) (identification name/number)

 Equipment/process(es) controlled. Include emission point 

designations (e.g., E3, E4 from plot plan)

 Latitude (decimal degrees, six decimal places)

 Longitude (decimal degrees, six decimal places)

 Stack or vent height (units)

 Stack or vent diameter (units)

 For general or building ventilation:

 Ventilation system used

 Airflow control system used

 Number of air changes per hour

 For unit or local ventilation:

 Enclosure or hood design used

 Volume of enclosure or hood

 Capture velocity (ft/sec)

 Distance between hood and emission source (ft)
FORM C-9

AIR POLLUTION CONTROL

IX. Other (none)

 For each other air pollution control devide (APCD): Other APCD 1 Other APCD 2 Other APCD 3

 Process line(s) (identification name/number)

 Equipment/process(es) controlled. Include emission point 

designations (e.g., E3, E4 from plot plan)

 Latitude (decimal degrees, six decimal places)

 Longitude (decimal degrees, six decimal places)

 Stack or vent height (units)

 Stack or vent diameter (units)

 Description
FORM D

PROCESS LINE STARTUP AND SHUTDOWN

1. For each startup and shutdown (SS) that occurred during the past 

five years, please provide the following information requested in A. 

through J. 

 A. Using the definitions provided above, indicate whether the 

event was a startup or shutdown; None

 B. A description of the event, including identification of the 

emissions source or sources associated with the startup or 

shutdown; None

 C. Whether any permit condition was exceeded and, if so, what 

permit condition was exceeded; None

 D. Whether the event was covered by any contingency plan for 

controlling emissions during startup and shutdown events and, if so, 

whether the plan was followed; if the plan was not followed, why not; None

 E. The duration of the event; NA

 F. The actions taken to minimize emissions during the event, 

including the use of any backup control systems; None

 G. Estimates or measurements, if any, of emissions during the 

event; if you did not have the ability to quantify emissions during the 

event, please explain why; None

 H. Whether the emission profile of each unit was different during 

startup and shutdown than during normal operating conditions and, if 

so, how emissions were different and why; please provide any

supporting information; NA

 I. All performance test data collected during each period of SS; 

the test method used for each event; when the testing was 

conducted and why; the test conditions at the time of testing; and 

whether the tests were associated with a routine startup or shutdown; 

and NA

 J. All monitoring data, including control system parameter 

monitoring, collected during each period of SS. NA

Startup: the setting in operation of an affected source or portion of an affected source for any purpose.

Shutdown: the cessation of operation of an affected source or portion of an affected source for any purpose.
If this information is contained in periodic and immediate SS reports 

(either stand-alone or contained within the periodic excess emissions 

report) submitted to your permitting authority, you may submit copies 

of those reports instead.

2. Are there any types of startup or shutdown events that you have 

been able to eliminate? If so, please describe the type of event and 

explain how these events were eliminated. None

3. Please submit a copy of your SS plan if you are required to 

develop one. Attached

4. Please provide all performance test data collected during periods 

of SS over the last 5 years. Indicate the test method used for each 

event. Attached

5. Please provide all monitoring data, including control system 

parameter monitoring, collected during periods of SS over the last 5 

years. Attached

6. Optional: Do you wish to recommend a standard that would apply

during startup or shutdown? If so, please describe the event to 

which the standard would apply; the recommended standard (this 

could be an emission limitation, work practice, or operational 

standard) that would apply during the period; the basis for the 

recommended standard; why and how the standard would minimize 

emissions during the event; and how would compliance be 

determined and/or monitored. None
FORM E

PRESENCE OF AIR POLLUTANTS IN EMISSION POINTS

(testing 

reported 

separately)

Please provide any existing emissions information and data covering 

hazardous air pollutants (HAP), particulate matter (PM), and carbon 

monoxide (CO) for each listed process. Identify the appropriote box for 

which you are providing specific process inofrmation and/or pollutant 

emissions data.

Cupola Fiberization Fiber Collection Curing Cooling

Carbon monoxide (CO)

Carbonyl sulfide (COS)

Particulate Matter (PM, PM2.5, PM10, PM condensable) 

Chromium compounds and Hexavalent Chromium (including any Cr 

speciation data)

Other metal HAP (As, Be, Cd, Co, Hg, Pb, Mn, Sb, Se)

Hydrogen Fluoride (HF)

Hydrogen Chloride (HCl)

Formaldehyde

Phenol

Methanol

Other organic HAP
FORM F-1 

COST

I. Process Unit (e.g., cupola, curing oven, etc.):

 For each process unit: Process Unit 1 Process Unit 2 Process Unit 3

 Process Unit ID

 Process Line ID

II. Capital Costs

 Base year

 Total capital cost, including costs for individual pieces, if available.

III. Annual Operating Costs

 Base year (most recent fiscal year)

 Total annual operating costs

 Maintenance materials and replacement parts (specify costs by

item)

 Raw materials costs

 Labor

 ($/yr) for each labor class

 (hr/hr) for each labor class

 Utilities (breakdown for each utility)

 Waste treatment and/or disposal

 Costs associated with any work practices and pollution prevention 

techniques that are employed at your facility

 Savings associated with heat recovery and wastewater and/or solid 

waste returned to process from APCD (or sold to another user)

 Indirect costs

 Other (specify)

Please provide the annual report to shareholders or equivalent for 

the most recent fiscal year. If reports are not available, provide 

annual sales and profits (or profit margin) for the most recent fiscal 

year. If company is publicly owned, please provide a web link to this 

information.

Identify the market range (regional, national, international) of your 

products.
Can your product(s) be substituted by another product(s)? If so, 

please list your product(s) and substituted product(s).
FORM F-2 

COST

I. Air Pollution Control Device (APCD)

 For each APCD: APCD 1 APCD 2 APCD 3

 APCD ID

 Process Unit ID

II. Capital Costs

 Base year

 APCD equipment purchase cost and what was included

 List the cost for each piece of auxiliary equipment for each APCD not 

included above

 Installation cost

 Land purchase cost

 Total capital cost

 Method of financing APCD

 Retrofit installation

 Field erected or modular

III. Annual Operating Costs

 Base year (most recent fiscal year)

 Maintenance materials and replacement parts (specify costs by item)

 Raw materials costs

 Labor

 ($/yr) for each labor class

 (hr/hr) for each labor class

 Utilities (breakdown for each utility)

 Waste treatment and/or disposal

 Indirect costs

 Other (specify)

 Total annual operating cost (most recent fiscal year)

Attach annual report to shareholders or equivalent for the most recent 

fiscal year