FORM A-1

PARENT COMPANY INFORMATIONI. Parent Company / Legal Corporate Owner Information 1. Legal Parent Company / Legal Corporate Name Owens Corning Insulating Systems, LLC 2. Address One Owens Corning Parkway 3. City Toledo 4. State Ohio 5. Zip Code 43659 6. County Lucas 7. Size of Company (approximate number of employees including all subsidiaries, branches, and related establishments owned):

16,280
FORM A-2

FACILITY INFORMATIONII. Facility Information Facility Name Owens Corning Insulating Systems, LLC Facility Address Street 3700 North Interstate 35 East City Waxahachie State Texas Zip Code 75165 7. Size of Company (approximate number of employees including all subsidiaries, branches, and r Ellis elated establishments ow Facility Coordinates Latitude (decimal degrees, six decimal places) 32.441478 Longitude (decimal degrees, six decimal places) 96.848342 Specific location represented (e.g., front door of main building, centroid of property, etc.)

Centroid of Property

 Number of employees attached to the wool fiberglass manufacturing 

facility:

346

 Design capacity of the plant (tons/yr) Type(s) of process(es) (rotary spin, flame attenuation) at this plant Rotary Spin Operation schedule

24

 days/yr 365 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)

Applicable requirements referenced in Title V PermOperating Permit 6093. Provided on CD.

III. Technical Contact Name Mike Pettis Technical Contact Title ISB Environmental Leader Telephone 740-877-7087 Facsimile (Fax) 740-328-2696 Email Mike.Pettis@owenscorning.com
FORM A-2

FACILITY INFORMATIONIV. Other Is the facility a major source of HAP? Yes, currently. If No, did the facility take a limit of its potential HAP emissions to avoid classification as a major source:

N/A

 Does the facility manufacture other products in addition to wool 

fiberglass?

No

 If Yes, list the other products manufactured at the facility. N/A Are there any HAP emissions associated with any co-located facilities? List unit operations, e.g., boiler, and pollutant/emissions.

N/A
FORM B-1

PLANT OPERATIONSI. Overview of Plant OperationsNumber of process lines. Include lines that are currently operational or that are temporarily shutdown. (Do not include lines permanently shutdown).

3

For each process line: Process Line 1 Process Line 2 Process Line 3 Process line identification names or numbers V1 V2 V3 Type of process line (e.g., rotary spin, flame attenuation) Rotary Spin Rotary Spin Rotary Spin Maximum annual production rate (tons/yr) 7. Size of Company (approximate number of employees including all subsidiaries, branches, and related establishments owned):

47 37 32

 Remaining economic life of process line (yrs) N/A. Continued 

maintenance can maintain indefinite life.

N/A. Continued maintenance can maintain indefinite life.

N/A. Continued maintenance can maintain indefinite lif

 List of products produced and most recent annual production (tons/yr; specify year) for each productPlease attach detailed schematics of each process line. Provided on CD. Provided on CD. Provided on CD.
FORM B-2

PLANT OPERATIONSII. Process - Raw materials Handling and Storage Molten glass preparation Raw materials and proportions by wt (%) Industry information provided for representativeness. 

Soda ash (9%), Borax (12%), Cullet (34%), Limestone

(9%) and Sand (31%).

 Method(s) of conveying each raw material to furnace/pots Raw materials are unloaded and conveyed into a bucket 

elevator, which carries raw materials to individual storage 

silos. From the silos batch materials are gravity fed into a scale hopper and then into a mixer. For V2/V3 the mixed 

batch is pneumatically conveyed to mixed batch storage 

silos. The mixed batch is auger fed into the batch chargesurge hopper and then gravity feeds into the batch charger hopper. Batch is delivered into the V2 and V3 furnaces from the batch charger. For V1 the mixed batch dumps onto a transport conveyor and is mechanicallyconveyed to the mixed batch storage silos. The mixed batch is gravity fed into the V1 batch chargers and then auger feeds into the melter.

Binder and Additives

 List each raw material, including premixed materials, in the binder formulation and its proportion by wt (%) List steps in preparing binder, including storage temperature (°F) 

and holding time (hrs)

The above listed binder ingredients are metered into 

binder mix tanks. Mixed binder is transferred to arecirculating tank. All storage temperatures are ambient. 

Total holding time is approximately 45 minutes.

 7. Size of Company (approximate number of employees including all subsidiaries, branches, and related establishments 

owned): Cost of binder ($/gal) for most recent year (specify year) Are binder storage and mixing tanks vented to outside/inside? Binder storage tanks are vented inside and the binder 

mixing tanks are vented outside.

 Method of treating vent air from storage and mix tanks N/A Emission control during liquid raw material transfer from vehicles to storage tanks.

N/A
FORM B-2

PLANT OPERATIONSII. Process - Raw materials Handling and Storage Describe future source reduction plans and schedules to reformulate binders; List each constituent, proportions wt (%), cost ($/gal) for reformulation
FORM B-3

PLANT OPERATIONSIII. Process - Glass Melting Furnace For each Glass Melting Furnace: Furnace 1 Furnace 2  Process unit identification name/number V1 Furnace (01MELT) V2 Furnace (02MELT) V3 F Process line(s) served (identification name/number) V1 V2 V3  Latitude (decimal degrees, six decimal places) 32.4399942 32.4396072 (east) and 

32.4396492

32.432.4

 Longitude (decimal degrees, six decimal places) -96.8497775 -96.8491411 (east) and -

96.8492286

-96.96.8

 Stack or vent height (units) 53.42 ft 57.78 ft. (each) 57.4

(we

 7. Size of Company (approximate number of employees including all subsidiaries, branches, and related establishments owned):

2.92 ft. 4.00 ft. (each) 4.00 

 Manufacturer and model Oxy-Fuel Cold Top Cold  Date of original installation 1999 1973 197 Estimate of remaining lifetime (yrs) N/A. Continued maintenance 

can maintain indefinite life.

N/A. Continued maintenance can maintain indefinite life.

N/Acan 

 Major rebuilds: What constitutes a major rebuild Frequency of a major rebuild N/A N/A N/A Cost of typical major rebuild N/A N/A N/A Date of last major rebuild N/A N/A N/A Purpose of last major rebuild N/A N/A N/A Increase or decrease in emissions N/A N/A N/A Fuel type: electric, gas, or oil Gas/Oxy Electric heat with Natural Gas 

boost

Elecboo

 Fuel consumption rate (KW/ton of glass or Btu/ton of glass)

Chromium Compounds Chromium Compounds Chr

 Design production rate (tons/day) Actual glass pull rate (tons/day) Vent gas flow rate (acfm @ °F) Temperature (°F) of molten glass in furnace and forehearth (if applicable)
FORM B-3

PLANT OPERATIONSIII. Process - Glass Melting Furnace For each Glass Melting Furnace: Furnace 1 Furnace 2  Process unit identification name/number V1 Furnace (01MELT) V2 Furnace (02MELT) V3 F Process line(s) served (identification name/number) V1 V2 V3  Nature and frequency of routine/preventive maintenance procedures

Daily, visible inspection of batch charge operations, 

furnace condition and burner / oxygen supply system. Repairs and replacements are routinely completed when need is identified. General maintenance activities follow a prescribed schedule that is detailed in the maintenance tracking system. Refractory repairs are completed infrequently and only as necessary. 

General maintenance activities follow a prescribed 

schedule that is detailed in the maintenance tracking system. Basic, routine repairs and replacements are performed weekly for the batch charger. Repairs to the electrical systems, which includes electrodes and regulating transformers, are completed every 30 days. Refractory repairs are completed infrequently and only as necessary.

Genactiv

schemaiBasreplweeRepsystelectraneverepainfrenec

 Describe process modification(s) since 1999 that reduce emissions

The Company has established goals to reduce the environmental footprint of our manufacturing operations as part of our sustainability efforts. These goals are focused on reducing waste-tolandfill, GHG, water consumption, VOC's, particulate matter, NOx and energy.

The Company has established goals to reduce the environmental footprint of our manufacturing operations as part of our sustainability efforts. These goals are focused on reducing waste-tolandfill, GHG, water consumption, VOC's, particulate matter, NOx and energy. Installed batch wetting.

The estathe our as peffofoculandconpartenewett

 Describe future source reduction plans and schedules None currently approved or 

scheduled at this time.

None currently approved or scheduled at this time.

Nonsche
FORM B-4

PLANT OPERATIONSIV. Process - Forming -- Rotary Spin / Flame Attenuation For each Forming Operation -- Rotary Spin/Flame Attenuation Forming Operation 1 Forming Operation  Process unit identification name/number V1 Forming (01FORM) V2 Forming (02FORM) Process line(s) served (identification name/number) V1 V2  Latitude (decimal degrees, six decimal places) 32.4401553 32.4401 Longitude (decimal degrees, six decimal places) -96.8494169 -96.8489064 Stack or vent height (units) 63.50 ft. 76.33 ft. 7. Size of Company (approximate number of employees including all subsidiaries, branches, and related establishments owned):

9.78 ft. 10.50 ft.

 Number of fiber forming devices (spinners) per line. Method of attenuating fiber (e.g., air, flame, or air and flame). Indicate type of burner used (if flame).

Air and Flame Air and Flame

 Is there a forehearth between the furnace and the forming 

section?

Yes Yes

 Major rebuilds: What constitutes a major rebuild The company undertakes

routine repair and replacementprojects. As with the furnace,these projects are normally “asis” maintenance projects that donot impact the formingemissions. Therefore, thecompany does not considerthese to be major rebuilds forthe purpose of this ICR.

The company undroutine repair and replaprojects. As with the these projects are normis” maintenance projects not impact the emissions. Thereforecompany does not cthese to be major rebthe purpose of this ICR.

 Frequency of a major rebuild N/A N/A Cost of typical major rebuild N/A N/A Date of last major rebuild N/A N/A Purpose of last major rebuild N/A N/A Increase or decrease in emissions N/A N/A If modular, number of modules and plenums Presence of water overspray and application rate (gpm) Other material applied and application rate (gpm) None None
FORM B-4

PLANT OPERATIONSIV. Process - Forming -- Rotary Spin / Flame Attenuation For each Forming Operation -- Rotary Spin/Flame Attenuation Forming Operation 1 Forming Operation  Process unit identification name/number V1 Forming (01FORM) V2 Forming (02FORM) Process line(s) served (identification name/number) V1 V2  Temperature of glass fiber when binder is applied (°F) Temperature of binder when applied to fibers (°F) Method of evenly distributing fibers onto forming conveyor Compressed air lapping system Compressed air lapping 

 Formed mat thickness (in.) 1"-6" as formed, up to 15" on 

ramp.

1"-6" as formed, up to 1ramp.

 Forming air flow rate (acfm @ °F) Percent of forming air recirculated and percent exhausted None recirculated, 100% 

exhausted.

None recirculated, 100% exhausted.

 Nature and frequency of routine/preventive maintenance procedures

General maintenance activities follow a prescribed schedule that is detailed in the maintenance tracking system. Repairs and replacements are 

performed when required during unscheduled downtimes. Basic, routine cleaning occurs every 6 to 12 weeks. Significant repairs such as chain and sprocket replacement, frame repair and track replacement generally occur with refractory replacement of the furnace.

General maintenance acfollow a prescribed schethat is detailed in the maintenance tracking syRepairs and replacemen

performed when requireunscheduled downtimesBasic, routine cleaning oevery 6 to 12 weeks. Significant repairs such chain and sprocket replacement, frame repatrack replacement geneoccur with refractory replacement of the furna

 Describe process modification(s) since 1999 that reduce 

emissions Describe future source reduction plans and schedules None currently approved or 

scheduled at this time.

None currently approved scheduled at this time.
FORM B-4

PLANT OPERATIONSIV. Process - Forming -- Rotary Spin / Flame Attenuation For each Forming Operation -- Rotary Spin/Flame Attenuation Process unit identification name/number Process line(s) served (identification name/number) Latitude (decimal degrees, six decimal places) Longitude (decimal degrees, six decimal places) Stack or vent height (units) 7. Size of Company (approximate number of employees including all subsidiaries, branches, and related establishments owned): Number of fiber forming devices (spinners) per line. Method of attenuating fiber (e.g., air, flame, or air and flame). Indicate type of burner used (if flame). Is there a forehearth between the furnace and the forming section? Major rebuilds: What constitutes a major rebuild Frequency of a major rebuild Cost of typical major rebuild Date of last major rebuild Purpose of last major rebuild Increase or decrease in emissions If modular, number of modules and plenums Presence of water overspray and application rate (gpm) Other material applied and application rate (gpm)

Forming Operation 3

V3 Forming (03FORM)V3 32.4400536-96.848743961.92 ft.13.70 ft.Air and FlameYesThe company undertakesroutine repair and replacementprojects. As with the furnace,these projects are normally “asis” maintenance projects that donot impact the formingemissions. Therefore, thecompany does not considerthese to be major rebuilds forthe purpose of this ICR.N/AN/AN/AN/AN/ANone
FORM B-4

PLANT OPERATIONSIV. Process - Forming -- Rotary Spin / Flame Attenuation For each Forming Operation -- Rotary Spin/Flame Attenuation Process unit identification name/number Process line(s) served (identification name/number) Temperature of glass fiber when binder is applied (°F) Temperature of binder when applied to fibers (°F) Method of evenly distributing fibers onto forming conveyor Formed mat thickness (in.) Forming air flow rate (acfm @ °F) Percent of forming air recirculated and percent exhausted Nature and frequency of routine/preventive maintenance procedures Describe process modification(s) since 1999 that reduce emissions Describe future source reduction plans and schedules

Forming Operation 3

V3 Forming (03FORM)V3 Compressed air lapping system1"-6" as formed, up to 15" on ramp.None recirculated, 100% exhausted.General maintenance activities follow a prescribed schedule that is detailed in the maintenance tracking system. Repairs and replacements are performed when required during unscheduled downtimes. Basic, routine cleaning occurs every 6 to 12 weeks. Significant repairs such as chain and sprocket replacement, frame repair and track replacement generally occur with refractory replacement of the furnace.None currently approved or scheduled at this time.
FORM B-5

PLANT OPERATIONSV. Process - Curing  For each Curing Oven: Curing Oven 1 Curing Oven 2 Process unit identification name/number V1 Curing (01CURE) V2 Curing (02CURE) Process line(s) served (identification name/number) V1 V2 Latitude (decimal degrees, six decimal places) 32.4401553 32.4401 Longitude (decimal degrees, six decimal places) -96.8494169 -96.8489064 Stack or vent height (units) 63.50 ft. 76.33 ft. 7. Size of Company (approximate number of employees including all subsidiaries, branches, andrelated establishments owned):

9.78 ft. 10.50 ft.

 Method of curing  Manufacturer and model OC Proprietary Design OC Proprietary Design Date of original installation 1963 1973 Major rebuilds: What constitutes a major rebuild The company undertakes

routine repair and replacementprojects. As with the furnace,these projects are normally “asis” maintenance projects that donot impact the oven emissions.Therefore, the company doesnot consider these to be majorrebuilds for the purpose of thisICR.

The company undertakesroutine repair and replacementprojects. As with the furnace,these projects are normally “asis” maintenance projects that donot impact the oven emissions.Therefore, the company doesnot consider these to be majorrebuilds for the purpose of thisICR.

 Frequency of a major rebuild N/A N/A Cost of typical major rebuild N/A N/A Date of last major rebuild N/A N/A Purpose of last major rebuild N/A N/A Increase or decrease in emissions N/A N/A Fuel type: electric, gas, or oil Natural Gas Natural Gas Fuel consumption rate (KW/hr or BTU/hr) inlet 2.5 - 5% 2 - 4% outlet <0.5% <0.5%
FORM B-5

PLANT OPERATIONSV. Process - Curing  For each Curing Oven: Curing Oven 1 Curing Oven 2 Process unit identification name/number V1 Curing (01CURE) V2 Curing (02CURE) Process line(s) served (identification name/number) V1 V2 Air flow rate (acfm @ °F) from curing 26,000 acfm @ 450 °F 26,000 acfm @ 450 °F Exhaust air temperature (°F) 450 °F 450 °F Residence time of product (mins) Binder content of cured product (LOI) Nature and frequency of routine/preventive maintenance procedures

General maintenance activities follow a prescribed schedule that is detailed in the maintenance tracking system. Repairs and replacements are 

performed when required during unscheduled downtimes. Basic, routine cleaning occurs every 6 to 12 weeks. Significant repairs such as chain and sprocket replacement, frame repair and track replacement generally occur with refractory replacement of the furnace.

General maintenance activities follow a prescribed schedule that is detailed in the maintenance tracking system. Repairs and replacements are 

performed when required during unscheduled downtimes. Basic, routine cleaning occurs every 6 to 12 weeks. Significant repairs such as chain and sprocket replacement, frame repair and track replacement generally occur with refractory replacement of the furnace.

 Describe process modification(s) since 1999 that 

reduce emissions Describe future source reduction plans and schedules

None currently approved or scheduled at this time.

None currently approved or scheduled at this time.
FORM B-5

PLANT OPERATIONSV. Process - Curing  For each Curing Oven: Process unit identification name/number Process line(s) served (identification name/number) Latitude (decimal degrees, six decimal places) Longitude (decimal degrees, six decimal places) Stack or vent height (units) 7. Size of Company (approximate number of employees including all subsidiaries, branches, andrelated establishments owned): Method of curing  Manufacturer and model Date of original installation Major rebuilds: What constitutes a major rebuild Frequency of a major rebuild Cost of typical major rebuild Date of last major rebuild Purpose of last major rebuild Increase or decrease in emissions Fuel type: electric, gas, or oil  Fuel consumption rate (KW/hr or BTU/hr) inlet outlet

Curing Oven 3

V3 Curing (03CURE)V332.4400536-96.848743961.92 ft.13.70 ft.OC Proprietary Design1978The company undertakesroutine repair and replacementprojects. As with the furnace,these projects are normally “asis” maintenance projects that donot impact the oven emissions.Therefore, the company doesnot consider these to be majorrebuilds for the purpose of thisICR.N/AN/AN/AN/AN/ANatural Gas2 - 4%<0.5%
FORM B-5

PLANT OPERATIONSV. Process - Curing  For each Curing Oven: Process unit identification name/number Process line(s) served (identification name/number) Air flow rate (acfm @ °F) from curing Exhaust air temperature (°F) Residence time of product (mins) Binder content of cured product (LOI) Nature and frequency of routine/preventive maintenance procedures Describe process modification(s) since 1999 that reduce emissions Describe future source reduction plans and schedules

Curing Oven 3

V3 Curing (03CURE)V326,000 acfm @ 450 °F450 °FGeneral maintenance activities follow a prescribed schedule that is detailed in the maintenance tracking system. Repairs and replacements are performed when required during unscheduled downtimes. Basic, routine cleaning occurs every 6 to 12 weeks. Significant repairs such as chain and sprocket replacement, frame repair and track replacement generally occur with refractory replacement of the furnace.None currently approved or scheduled at this time.
FORM B-6

PLANT OPERATIONSVI. Process - Cooling For each Cooling Operation: Cooling Operation 1 Cooling Operation 2

 Process unit identification name/number V1 Cooling (01COOL) V2 Cooling (02COOL) Process line(s) served (identification name/number) V1 V2 

 Latitude (decimal degrees, six decimal places) 32.4403419 32.4403375 Longitude (decimal degrees, six decimal places) -96.8492069 -96.8487631 Stack or vent height (units) 45.75 ft 46.5 ft. 7. Size of Company (approximate number of employees including all subsidiaries, branches, andrelated establishments owned):

2.92 ft. 3.5 ft.

 Cooling air flow rate (acfm @ °F) 110,000 - 120,000 acfm @ 150 

°F

25,000 - 35,000 acfm @ 112 °F

 Percentage of cooling air recirculated (if any) None None  Cooling air temperature (°F) 120 - 150 °F 100 - 150 °F Nature and frequency of routine/preventive maintenance procedures

General maintenance activities follow a prescribed schedule that is detailed in the maintenance tracking system. Repairs and replacements are 

performed when required during unscheduled downtimes. Basic, routine cleaning occurs every 6 to 12 weeks. Significant repairs such as chain and sprocket replacement, frame repair and track replacement generally occur with refractory replacement of the furnace.

General maintenance activities follow a prescribed schedule that is detailed in the maintenance tracking system. Repairs and replacements are 

performed when required during unscheduled downtimes. Basic, routine cleaning occurs every 6 to 12 weeks. Significant repairs such as chain and sprocket replacement, frame repair and track replacement generally occur with refractory replacement of the furnace.

 Describe process modification(s) since 1999 that reduce emissions
FORM B-6

PLANT OPERATIONSVI. Process - Cooling For each Cooling Operation: Cooling Operation 1 Cooling Operation 2

 Process unit identification name/number V1 Cooling (01COOL) V2 Cooling (02COOL) Process line(s) served (identification name/number) V1 V2 

 Describe future source reduction plans and schedules None currently approved or 

scheduled at this time.

None currently approved or scheduled at this time.
FORM B-6

PLANT OPERATIONSVI. Process - Cooling For each Cooling Operation: Process unit identification name/number Process line(s) served (identification name/number) Latitude (decimal degrees, six decimal places) Longitude (decimal degrees, six decimal places) Stack or vent height (units) 7. Size of Company (approximate number of employees including all subsidiaries, branches, andrelated establishments owned): Cooling air flow rate (acfm @ °F) 

 Percentage of cooling air recirculated (if any) Cooling air temperature (°F) Nature and frequency of routine/preventive maintenance procedures Describe process modification(s) since 1999 that 

reduce emissions

Cooling Operation 3

V3 Cooling (03COOL)V3 

32.4402581-96.848544463.33 ft.3.5 ft.10,000 - 25,000 acfm @ 123 °FNone 100 - 150 °FGeneral maintenance activities follow a prescribed schedule that is detailed in the maintenance tracking system. Repairs and replacements are performed when required during unscheduled downtimes. Basic, routine cleaning occurs every 6 to 12 weeks. Significant repairs such as chain and sprocket replacement, frame repair and track replacement generally occur with refractory replacement of the furnace.
FORM B-6

PLANT OPERATIONSVI. Process - Cooling For each Cooling Operation: Process unit identification name/number Process line(s) served (identification name/number) Describe future source reduction plans and schedules

Cooling Operation 3

V3 Cooling (03COOL)V3 

None currently approved or scheduled at this time.
FORM B-7

PLANT OPERATIONSVII. Process - Use of Solvents Use of Solvents Volatile solvents used at your facility (where and how used) N/A. No HAP-containing solvents used in the 

manufacturing process.

 List each solvent used and quantity (gal/yr) N/A. No HAP-containing solvents used in the 

manufacturing process.

 Emission control device(s) used to control emissions from solvent usage/storage?

N/A. No HAP-containing solvents used in the manufacturing process.
FORM B-8

PROCESS OPERATIONSVIII. Pollution PreventionPlease 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 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.
FORM C-1

AIR POLLUTION CONTROLI. Electrostatic Precipitator (ESP) For each ESP: ESP 1 Process line(s) (identification name/number) V1 Furnace (01MELT) Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan)

V1 Furnace (01MELT)

 Latitude (decimal degrees, six decimal places) 32.4399942 Longitude (decimal degrees, six decimal places) -96.8497775 Stack or vent height (units) 53.42 ft 7. Size of Company (approximate number of employees including all subsidiaries, branches, and related establishments owned):

2.92 ft.

 Manufacturer and model Alstom Power 1 FTA 3x45F-35-

40

 Date of original installation 2000 Number of collection plates and configuration 90/field Gas flow rate to ESP (acfm @ °F) 19,792 acfm @ 408 °F Inlet gas temperature (°F) 408 °F Outlet gas temperature (°F) 389 °F Inlet grain loading (gr/dscf) 0.5271 gr/dscf Outlet grain loading (gr/dscf) 0.0180 gr/dscf Average stack opacity (%) <10% Pressure drop across ESP (in. H2O gauge) 3" Plate area (ft2) 16,276 ft2 Vendor guarantee on ESP efficiency (attach copy) Yes. Provided on CD.

Rappers. Periodic cleaning.

 Flow rate of plate wash water to ESP (gpm), if applicable N/A Temperature of plate wash water to ESP (°F), if applicable N/A Source of plate wash water used for cleaning, if applicable N/A Concentration (mg/l) of dissolved and suspended solids in plate wash water, if applicable

N/A

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

applicable

N/A

 Amount of wastewater generated (gpd), if applicable N/A Amount of wastewater recycled (gpd), if applicable N/A Amount of wastewater disposed of (gpd), if applicable N/A Method of wastewater disposal, if applicable N/A
FORM C-1

AIR POLLUTION CONTROLI. Electrostatic Precipitator (ESP) For each ESP: ESP 1 Process line(s) (identification name/number) V1 Furnace (01MELT) Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan)

V1 Furnace (01MELT)

 Quantity of solid waste collected (lbs/yr) 2,500 lbs. Small quantities of 

DEP residue becomes contaminated in the process 

and must be disposed.

 Quantity of solid waste recycled (lbs/yr) 0 lbs Quantity of solid waste disposed of (lbs/yr) 2,500 lbs Method of solid waste disposal Hazardous Waste Landfill Nature and frequency of routine/preventive maintenance procedures

General maintenance activities follow a prescribed schedule that is detailed in the maintenance tracking system. Systems are continuously monitored and notifications 

occur that initiate maintenance. SIR repair and replacement is conducted as needed. Electrode replacement occurs on a a12-15 year cycle.

 Problems experienced with control device within the last five years; how were problems solved?

As reported in Title V deviation reports: electrical malfunction / repaired and reset; mechanical malfunction / repaired; and equipment failure / repaired.

 Continuous monitoring method(s) used to monitor ESP 

performance, including parameters monitored

Secondary voltage and amperage of 3rd field.

 Describe any plans to replace or upgrade ESP None currently approved or 

scheduled at this time.
FORM C-2

AIR POLLUTION CONTROL Not applicable to this 

facility.

II. Scrubber For each Scrubber: Scrubber Process line(s) (identification name/number) N/A Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan)

N/A

 Latitude (decimal degrees, six decimal places) N/A Longitude (decimal degrees, six decimal places) N/A Stack or vent height (units) N/A 7. Size of Company (approximate number of employees including all subsidiaries, branches, and related establishments owned):

N/A

 Manufacturer and model N/A Date of original installation N/A Type (e.g., venturi, orifice) N/A Gas flow rate to scrubber (acfm @ °F) N/A

 Inlet gas temperature (°F) N/A

 Outlet gas temperature (°F) N/A

 Inlet grain loading (gr/dscf) N/A Outlet grain loading (gr/dscf) N/A Average stack opacity (%) N/A Water flow rate to scrubber (gpm) N/A Percent of scrubber water from recycled wastewater N/A

 Source of scrubbing water and type of pretreatment. Substance(s) added as part of pretreatment and amount used (gpm or lbs/hr)

N/AN/A

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

scrubbing water

N/A

 Scrubbing water temperature (°F) N/A

 Liquid/gas ratio (gal/103 acfm) N/A

 Pressure drop across scrubber (in. H2O gauge) N/A
FORM C-2

AIR POLLUTION CONTROL Not applicable to this 

facility.

II. Scrubber For each Scrubber: Scrubber Process line(s) (identification name/number) N/A Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan)

N/A

 Amount of wastewater generated (gpd) N/A Amount of wastewater recycled (gpd) N/A Amount of wastewater disposed of (gpd) N/A Method of wastewater disposal N/A Quantity of solid waste collected (lbs/yr) N/A Quantity of solid waste recycled (lbs/yr) N/A Quantity of solid waste disposed of (lbs/yr) N/A Method of solid waste disposal N/A Vendor guarantee on scrubber efficiency (attach copy) N/A Nature and frequency of preventive maintenance procedures N/A Problems experienced with control device within the last five years; how were problems solved?

N/A

 Continuous monitoring method(s) used to monitor scrubber 

performance, including parameters monitored

N/A

 Plans to replace or upgrade scrubber N/A
FORM C-3

AIR POLLUTION CONTROLIII. Mechanical Collector Not applicable to this 

facility.

 For each Mechanical Collector: Mechanical Collector Process line(s) (identification name/number) N/A Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan)

N/A

 Latitude (decimal degrees, six decimal places) N/A Longitude (decimal degrees, six decimal places) N/A Stack or vent height (units) N/A Stack or vent diameter (units) N/A Manufacturer and model N/A Date of original installation N/A Type of mechanical collector N/A Gas flow rate to collector (acfm @ °F) N/A

 Inlet gas temperature (°F) N/A

 Outlet gas temperature (°F) N/A

 Inlet grain loading (gr/dscf) N/A Outlet grain loading (gr/dscf) N/A Average stack opacity (%) N/A Overall pressure drop (in. H2O gauge) N/A

 Vendor guarantee on mechanical collector efficiency (attach 

copy)

N/A

 Quantity of solid waste collected (lbs/yr) N/A Quantity of solid waste recycled (lbs/yr) N/A Quantity of solid waste disposed of (lbs/yr) N/A Method of solid waste disposal N/A Nature and frequency of preventive maintenance procedures N/A Problems experienced with control device within the last five 

years; how were problems solved?

N/A

 Continuous monitoring method(s) used to monitor performance, 

including parameters monitored

N/A

 Plans to replace or upgrade mechanical collector N/A
FORM C-4

AIR POLLUTION CONTROLIV. Fabric Filter  For each Fabric Filter: Fabric Filter 1 Fabric Filter 2  Process line(s) (identification name/number) V1 V2 V2 Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan)

V1 Mix Batch Storage Bin and Transfer Conveyor 

(stack 7)

V2 Mix Batch Storage Bin V2 Batc

 Latitude (decimal degrees, six decimal places) 32.4397278 32.4395364 32.4395 Longitude (decimal degrees, six decimal places) -96.8496564 -96.8491253 -96.849

 Stack or vent height (units) 79.78 ft. 61.37 ft. 65.53 ft 7. Size of Company (approximate number of employees including all subsidiaries, branches, andrelated establishments owned):

0.55 ft. 0.75 ft. 0.42 ft.

 Manufacturer and model Farr Model GS-1 Flex Kleen Model 58-BVBS16 III G Flex Kle

16 III G

 Date of original installation 2008 1972 1991 Number of compartments 1 1 1 Number of bags per compartment 1 37 37 Filter material and coatings applied Non-Woven Spun Bonded 

Polyester Media - Teflon 

Coated (PTFE)

Polyester - No Coating Polyeste

 Fabric weight (oz/yd2) 8 16 16

 Filter surface area (ft2) 200 ft2 No data available. 348 ft2

 Gas flow rate to filter (acfm @ °F) 300 acfm @ 100 °F No data available. 600 acfm 

 Inlet gas temperature (°F) Ambient Ambient Ambien

 Outlet gas temperature (°F) Ambient Ambient Ambien

 Inlet grain loading (gr/dscf) No data available. No data available. No data  Outlet grain loading (gr/dscf) No data available. No data available. No data 

 <5% <5% <5%

 Overall pressure drop (in. H2O gauge) 10" No data available. 10"
FORM C-4

AIR POLLUTION CONTROLIV. Fabric Filter  For each Fabric Filter: Fabric Filter 1 Fabric Filter 2  Process line(s) (identification name/number) V1 V2 V2 Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan)

V1 Mix Batch Storage Bin and Transfer Conveyor 

(stack 7)

V2 Mix Batch Storage Bin V2 Batc

 Method and frequency of bag cleaning Reversed compressed air. 

Compressed air by solenoids on a variable timer.

Reversed compressed air. Compressed air by solenoids on a variable timer.

ReverseCompreon a var

 Vendor guarantee on fabric filter efficiency (attach 

copy)

None provided. None provided. None pr

 Quantity of solid waste collected (lbs/yr) N/A (Closed system returns 

collected dust to process.)

N/A (Closed system returns collected dust to process.)

N/A (Clocollecte

 Quantity of solid waste recycled (lbs/yr) N/A (Closed system returns 

collected dust to process.)

N/A (Closed system returns collected dust to process.)

N/A (Clocollecte

 Quantity of solid waste disposed of (lbs/yr) 0 lbs 0 lbs 0 lbs Method of solid waste disposal N/A N/A N/A Nature and frequency of preventive maintenance procedures

General maintenance repairs as needed. Visual inspections and differential pressure checks are performed routinely. Bag or cartridge replacement is 

performed as needed.

General maintenance repairs as needed. Visual inspections and differential pressure checks are performed routinely. Bag or cartridge replacement is performed as needed.

Generaas needinspectipressurperformcartridge perform

 Problems experienced with control device within the last five years; how were problems solved?

None reported in Title V deviation reports. 

None reported in Title V deviation reports. 

None redeviatio

 Continuous monitoring method(s) used to monitor performance, including parameters monitored

N/A N/A N/A

 Plans to replace or upgrade fabric filter None currently approved or 

scheduled at this time.

None currently approved or scheduled at this time.

None cuschedul
FORM C-4

AIR POLLUTION CONTROLIV. Fabric Filter  For each Fabric Filter: 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) 7. Size of Company (approximate number of employees including all subsidiaries, branches, andrelated establishments owned): Manufacturer and model Date of original installation Number of compartments Number of bags per compartment Filter material and coatings applied Fabric weight (oz/yd2)

 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) Overall pressure drop (in. H2O gauge)

Fabric Filter 4 Fabric Filter 5

V3 V3V3 Mix Batch Storage Bin V3 Batch Charger32.4395042 (east) and 

32.4395147 (west)

32.4394747

-96.8490314 (east) and -

96.8490539 (west)

-96.8490097

79.03 ft. (each) 55.78 ft.0.78 ft. (each) 0.42 ft.Flex Kleen Model 58-BVBS16 III G Flex Kleen Model 58-BVBS- 16 III G1978 19911 (each) 1 (each)45 (each) 16 (each)Polyester - No Coating Polyester - No Coating16 16424 ft2 (each) 230 ft2 (each)

No data available. 400 acfm @ 100 °FAmbient AmbientAmbient AmbientNo data available. No data available.No data available. No data available. <5% <5%No data available. 10"
FORM C-4

AIR POLLUTION CONTROLIV. Fabric Filter  For each Fabric Filter: Process line(s) (identification name/number) Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan) 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 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 fabric filter

Fabric Filter 4 Fabric Filter 5

V3 V3V3 Mix Batch Storage Bin V3 Batch Charger

Reversed compressed air. Compressed air by solenoids on a variable timer.

Reversed compressed air. Compressed air by solenoids on a variable timer.

None provided. None provided.N/A (Closed system returns collected dust to process.)

N/A (Closed system returns collected dust to process.)

N/A (Closed system returns collected dust to process.)

N/A (Closed system returns collected dust to process.)

0 lbs 0 lbsN/A N/AGeneral maintenance repairs as needed. Visual inspections and differential pressure checks are performed routinely. Bag or cartridge replacement is performed as needed.

General maintenance repairs as needed. Visual inspections and differential pressure checks are performed routinely. Bag or cartridge replacement is performed as needed.

None reported in Title V deviation reports. 

None reported in Title V deviation reports. 

N/A N/ANone currently approved or scheduled at this time.

None currently approved or scheduled at this time.
FORM C-5

AIR POLLUTION CONTROLV. Thermal Incinerator For each Thermal Incinerator: Thermal Incinerator 1 Thermal Incinerator 2 T Process line(s) (identification name/number) V1 V2 V3 Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan)

V1 Curing (01CURE, 01INCIN) : Combined Exhaust (Forming/Curing) from Mixing 

Chamber

V2 Curing (02CURE, 02INCIN) : Combined Exhaust (Forming/Curing) from Mixing Chamber

V3 C03INC(FormCham

 Latitude (decimal degrees, six decimal places) 32.4401553 32.4401 32.44 Longitude (decimal degrees, six decimal places) -96.8494169 -96.8489064 -96.8 Stack or vent height (units) 63.50 ft. 76.33 ft. 61.92  7. Size of Company (approximate number of employees including all subsidiaries, branches, andrelated establishments owned):

9.78 ft. 10.50 ft. 13.70 

 Manufacturer and model HIRT Combustion TXL-18M- 48-X Bigelow/Liptak HIRT 

48

 Date of original installation 1980 1973 1978 Fuel type: gas or oil Natural Gas Natural Gas Natur Fuel consumption rate (BTU/hr) 7,240,000 BTU/hr 8,800,000 BTU/hr 4,050 Inlet gas flow rate (acfm @ °F) 26,000 acfm @ 100 °F 26,000 acfm @ 100 °F 26,00

 Inlet gas temperature (°F) 450 °F 450 °F 450 °

 Combustion chamber gas temperature (°F) 1300 °F 1300 °F 1300 

 Outlet gas temperature (°F) 1300 °F 1300 °F 1300 

 Inlet grain loading (gr/dscf) No data available. No data available. No da Outlet grain loading (gr/dscf) No data available. No data available. No da Average stack opacity (%) <15% <15% <15% Excess air (%) 0% 0% 0%

0.5 seconds at 1320 °F 2.2 seconds at 1300 °F 0.5 se

 Percent heat recovery 48% 0% 48% Vendor guarantee on incinerator efficiency (attach 

copy)

None provided. None provided. None 
FORM C-5

AIR POLLUTION CONTROLV. Thermal Incinerator For each Thermal Incinerator: Thermal Incinerator 1 Thermal Incinerator 2 T Process line(s) (identification name/number) V1 V2 V3 Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan)

V1 Curing (01CURE, 01INCIN) : Combined Exhaust (Forming/Curing) from Mixing 

Chamber

V2 Curing (02CURE, 02INCIN) : Combined Exhaust (Forming/Curing) from Mixing Chamber

V3 C03INC(FormCham

 Nature and frequency of preventive maintenance procedures

Annual inspections performed per MACT requirement and repairs made as needed.

Annual inspections performed per MACT requirement and repairs made as needed.

Annuper Mrepai

 Problems experienced with control device within the last five years; how were problems solved?

None reported in Title V deviation reports. 

As reported in Title V deviation reports: installation of new burner caused high NOX / modifications to burner control system; temperature setpoint malfunction / adjusted burner damper controls; burner flame failure / burner damper control and maintenance activities; and unable to maintain incinerator temperature / burner damper control and maintenance activities.

As rereporburnemaint

 Continuous monitoring method(s) used to monitor incinerator performance, including parameters monitored

Firebox temperature. Firebox temperature. Fireb

 Plans to replace or upgrade thermal incinerator None currently approved or 

scheduled at this time.

None currently approved or scheduled at this time.

None sched
FORM C-6

AIR POLLUTION CONTROLVI. High Velocity Air Filter (HVAF) For each HVAF: HVAF 1 HVAF 2  Process line(s) (identification name/number) V1 V2 V2  Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan)

V1 Cooling (01COOL) (HEAF) Unit

V2 Stripping (02STRIP) (Smoke Stripper)

V2 Co

 Latitude (decimal degrees, six decimal places) 32.4403419 32.4403558 32.44 Longitude (decimal degrees, six decimal places) -96.8492069 -96.8489 -96.8 Stack or vent height (units) 45.75 ft. 36.08 ft. 46.5 f 7. Size of Company (approximate number of employees including all subsidiaries, branches, andrelated establishments owned):

2.92 ft. 1.25 ft. 3.5 ft

 Manufacturer and model OC Proprietary Design OC Proprietary Design Whee Date of original installation 1975 1975 1973 Inlet gas flow rate (acfm @ °F) 10,000 - 15,000 acfm @ 152 

°F

1,000 - 3,000 acfm @ 169 °F 25,00

°F

 Inlet gas temperature (°F) 100 - 120 °F 110 - 120 °F 100 - 

 Outlet gas temperature (°F) 100 - 150 °F 100 - 150 °F 100 - 

 Inlet grain loading (gr/dscf) No data available. No data available. No da Outlet grain loading (gr/dscf) No data available. No data available. No da Average stack opacity (%) <20% <20% <20% Water spray pressure (sdig), if applicable 30-40 psig 50 psig 30-40  Water spray rate (gpm), if applicable No data available. 10 - 20 gpm No da Filter face velocity (acfm/ft2) No data available. 90-310 acfm/ft2 No da

 Maximum pressure drop across mat (in. H2O gauge) 25-30" 25-30" 25-30

N/A N/A None 

 Method and frequency of filter mad advancement Automatic feed based on 

differential pressure.

Manually, once per shift. Autom

differ

 Amount of wastewater generated (gpd) 0 gpd 0 gpd 0 gpd Amount of wastewater recycled (gpd) 100% 100% 100% Amount of wastewater disposed of (gpd) 0 gpd 0 gpd 0 gpd
FORM C-6

AIR POLLUTION CONTROLVI. High Velocity Air Filter (HVAF) For each HVAF: HVAF 1 HVAF 2  Process line(s) (identification name/number) V1 V2 V2  Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan)

V1 Cooling (01COOL) (HEAF) Unit

V2 Stripping (02STRIP) (Smoke Stripper)

V2 Co

 Method of wastewater disposal N/A N/A N/A Quantity of solid waste collected (lbs/yr) No data available. 39,000 lbs/yr No da Quantity of solid waste recycled (lbs/yr) 0 lbs/yr 0 lbs/yr 0 lbs/ Quantity of solid waste disposed of (lbs/yr) No data available. 39,000 lbs/yr No da Method of solid waste disposal Local Solid Waste Landfill Local Solid Waste Landfill Local 

 Nature and frequency of preventive maintenance procedures

General maintenance activities follow a prescribed schedule that is detailed in the maintenance tracking system. Cleaning is performed on a cycle matched to machine downtime.

General maintenance activities follow a prescribed schedule that is detailed in the maintenance tracking system. Nozzles and flow patterns are checked daily; repairs are completed as needed. Cleaning is performed on a cycle matching machine downtime.

Genefollow that is maintCleancycle down

 Problems experienced with control device within the 

last five years; how were problems solved?

None reported in Title V deviation reports. 

None reported in Title V deviation reports. 

None devia

 Continuous monitoring method(s) used to monitor HVAF performance, including parameters monitored

N/A N/A N/A

 Plans to replace or upgrade HVAF None currently approved or 

scheduled at this time.

None currently approved or scheduled at this time.

None sched
FORM C-6

AIR POLLUTION CONTROLVI. High Velocity Air Filter (HVAF) For each HVAF: 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) 7. Size of Company (approximate number of employees including all subsidiaries, branches, andrelated establishments owned): 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 (sdig), if applicable Water spray rate (gpm), if applicable Filter face velocity (acfm/ft2)

 Maximum pressure drop across mat (in. H2O gauge)

 Method and frequency of filter mad advancement Amount of wastewater generated (gpd) Amount of wastewater recycled (gpd) Amount of wastewater disposed of (gpd)

HVAF 4 HVAF 5

V3 V3 V3 Stripping (03STRIP) (Smoke Stripper)

V3 Cooling (03COOL) (HEAF)

32.4401578 32.4402581-96.8484139 -96.848544440.5 ft. 63.33 ft.1.17 ft 3.5 ft.OC proprietary design Anderson 2000/DF-44-IV1978 19783,000 - 5,000 acfm @ 120-160 °F

10,000 - 15,000 acfm @ 123 °F

110 - 120 °F 100 - 120 °F100 - 150 °F 100 - 150 °FNo data available. No data available.No data available. No data available.<20% <20%50 psig 30-40 psig10 - 20 gpm No data available.90-310 acfm/ft2 No data available.

25-30" 25-30"N/A None provided.Manually, once per shift. Automatic feed based on 

differential pressure.

0 gpd 0 gpd100% 100%0 gpd 0 gpd
FORM C-6

AIR POLLUTION CONTROLVI. High Velocity Air Filter (HVAF) For each HVAF: Process line(s) (identification name/number) Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan) 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

HVAF 4 HVAF 5

V3 V3 V3 Stripping (03STRIP) (Smoke Stripper)

V3 Cooling (03COOL) (HEAF)

N/A N/A39,000 lbs/yr No data available.0 lbs/yr 0 lbs/yr39,000 lbs/yr No data available.Local Solid Waste Landfill Local Solid Waste LandfillGeneral maintenance activities follow a prescribed schedule that is detailed in the maintenance tracking system. Nozzles and flow patterns are checked daily; repairs are completed as needed. Cleaning is performed on a cycle matching machine downtime.

General maintenance activities follow a prescribed schedule that is detailed in the maintenance tracking system. Cleaning is performed on a cycle matched to machine downtime.

None reported in Title V 

deviation reports. 

None reported in Title V deviation reports. 

N/A N/ANone currently approved or scheduled at this time.

None currently approved or scheduled at this time.
FORM C-7

AIR POLLUTION CONTROLVII. Mist Eliminator Not applicable to this facility. For each Mist Eliminator: Mist Eliminator Process line(s) (identification name/number) N/A Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 plot plan)

N/A

 Latitude (decimal degrees, six decimal places) N/A Longitude (decimal degrees, six decimal places) N/A Stack or vent height (units) N/A 7. Size of Company (approximate number of employees including all subsidiaries, branches, and related establishments owned):

N/A

 Manufacturer and model N/A Date of original installation N/A Type of mist eliminator N/A Gas flow rate to mist eliminator (acfm @ °F) N/A

 Inlet gas temperature (°F) N/A

 Outlet gas temperature (°F) N/A

 Inlet grain loading (gr/dscf) N/A Outlet grain loading (gr/dscf) N/A Average stack opacity (%) N/A Velocity in mist eliminator (ft/sec) N/A Pressure drop (in. H2O gauge) N/A

 For chevron blade mist eliminators: N/A

N/A

 Washing frequency of blades N/A For mesh pad mist eliminators: N/A Number of pads or elements N/A Thickness of pad (in.) or element dimensions N/A Density of pad, (lb/ft3) N/A

 Washing frequency of pad N/A
FORM C-7

AIR POLLUTION CONTROLVII. Mist Eliminator Not applicable to this facility. For each Mist Eliminator: Mist Eliminator Vendor guarantee on mist eliminator efficiency (attach copy) N/A Amount of wastewater generated (gpd) N/A Amount of wastewater recycled (gpd) N/A Amount of wastewater disposed of (gpd) N/A Method of wastewater disposal N/A Quantity of solid waste collected (lbs/yr) N/A Quantity of solid waste recycled (lbs/yr) N/A Quantity of solid waste disposed of (lbs/yr) N/A Method of solid waste disposal N/A Nature and frequency of preventive maintenance procedures N/A Problems experienced with control device within the last five years; how were problems solved?

N/A

 Continuous monitoring method(s) used to monitor mist eliminator performance, including parameters monitored

N/A

 Plans to replace or upgrade mist eliminator N/A
FORM C-8

AIR POLLUTION CONTROLVIII. Ventilation System  For each Ventilation System: Ventilation System 1 Process line(s) (identification name/number) Furnace Hall Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan)

Fugitive / Furnace Vents

 Latitude (decimal degrees, six decimal places) Multiple Locations Longitude (decimal degrees, six decimal places) Multiple Locations Stack or vent height (units) Roof Height Stack or vent diameter (units) Multiple Locations For general or building ventilation: Ventilation system used Natural draft with wall 

and roof louvers

 Airflow control system used Manually adjusted. Number of air changes per hour Estimated at 4-6 air 

changes per hour.

 For unit or local ventilation: Enclosure or hood design used N/A Volume of enclosure or hood N/A Capture velocity (ft/sec) N/A Distance between hood and emission source (ft) N/A
FORM C-9

AIR POLLUTION CONTROLIX. Other  For each Other Air Pollution Control Device (APCD): Other APCD 1 Other APCD 2 Process line(s) (identification name/number) V1 V2  Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan)

V1 Forming (01FORM) V2 Furnace (02MELT)

 Latitude (decimal degrees, six decimal places) 32.4401553 32.4396072 (east) and 

32.4396492

 Longitude (decimal degrees, six decimal places) -96.8494169 -96.8491411 (east) and -

96.8492286

 Stack or vent height (units) 63.50 ft. 57.78 ft. (each) 7. Size of Company (approximate number of employees including all subsidiaries, branches, and related establishments owned):

9.78 ft. 4.00 ft. (each)

Description Drop Out Box / Penthouse Batch Wetting
FORM C-9

AIR POLLUTION CONTROLIX. Other  For each Other Air Pollution Control Device (APCD): 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) 7. Size of Company (approximate number of employees including all subsidiaries, branches, and related establishments owned):

Description

Other APCD 3 Other APCD 4

V2 V3 V2 Forming (02FORM) V3 Furnace (03MELT)32.4401 32.4394836 (east) and 

32.4395267 (west)

-96.8489064 -96.8488961 (east) and -

96.8489864 (west)

76.33 ft. 57.45 ft.(east) and 57.28 ft. 

(west)

10.50 ft. 4.00 ft. (each)Drop Out Box / Penthouse Batch Wetting
FORM C-9

AIR POLLUTION CONTROLIX. Other  For each Other Air Pollution Control Device (APCD): 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) 7. Size of Company (approximate number of employees including all subsidiaries, branches, and related establishments owned):

Description

Other APCD 5

V3 V3 Forming (03FORM)32.4400536-96.848743961.92 ft.13.70 ft.Drop Out Box / Penthouse
FORM D

PROCESS LINE STARTUP AND SHUTDOWN 2005 - 2009 Semi-Annual MACT reports provided on CD.1. For each startup and shutdown (SS) that occurred during the last 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;

As indicated in the 2005 - 2009 Semi-Annual MACT Repo

 B. A description of the event, including identification of the emissions source or sources associated with the startup or 

shutdown;

As indicated in the 2005 - 2009 Semi-Annual MACT Repo

 7. Size of Company (approximate number of employees including all subsidiaries, branches, and related establishments 

owned):

As indicated in the 2005 - 2009 Semi-Annual MACT Repo

 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;

As indicated in the 2005 - 2009 Semi-Annual MACT Repo

 E. The duration of the event; As indicated in the 2005 - 2009 Semi-Annual MACT Repo F. The actions taken to minimize emissions during the event, including the use of any backup control systems;

As indicated in the 2005 - 2009 Semi-Annual MACT Repo

 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;

As indicated in the 2005 - 2009 Semi-Annual MACT Repo

 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;

As indicated in the 2005 - 2009 Semi-Annual MACT Repo

 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

No data available.

 J. All monitoring data, including control system parameter 

monitoring, collected during each period of SS.

As indicated in the 2005 - 2009 Semi-Annual MACT Repo

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.
FORM D

PROCESS LINE STARTUP AND SHUTDOWN 2005 - 2009 Semi-Annual MACT reports provided on CD.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.

No.

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

develop one.

As indicated in the 2005 - 2009 Semi-Annual MACT RepoNo data available.

5. Please provide all monitoring data, including control system parameter monitoring, collected during periods of SS over the last 5 years. 

As indicated in the 2005 - 2009 Semi-Annual MACT Repo

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. 

No.
FORM E

PRESENCE OF AIR POLLUTANTS IN EMISSION POINTSPlease provide any existing emissions information and data covering hazardous air pollutants (HAP) and particulate matter (PM) for each listed process. Identify the appropriate box for which you are providing specific process information and/or pollutant emissions data.

Melting Furnace Forming Curin

Particulate Matter (PM, PM 2.5, PM Condensable) 

Chromium Compounds and Hexavalent Chromium (including any Cr speciation data)Other metal HAP (As, Be, Cd, Co, Hg, Mn, Ni, Pb, Sb, Se)Hydrogen Fluoride (HF)Hydrogen Chloride (HCl)FormaldehydePhenolMethanolOther organic HAPThe existing data requested here has been provided to EPA by the industry’s trade association, the North 

American Insulation Manufacturers Association (“NAIMA”). The existing data provided by NAIMA was set forth in 

NAIMA’s May 5, 2010 letter to EPA. The existing emissions data provided from fiber glass companies included 

test results for the following pollutants: formaldehyde, methanol, phenol, particulate matter, hydrogen fluoride, 

metals (antimony, arsenic, beryllium, cadmium, chromium, cobalt, lead, manganese, nickel and selenium), 

mercury and hexavalent chromium. The existing emissions data provided from mineral wool companies included 

test results for the following pollutants: formaldehyde, methanol, phenol, particulate matter, carbon monoxide, carbonyl sulfide, hydrogen fluoride, metals (antimony, arsenic, beryllium, cadmium, chromium, cobalt, lead, 

manganese, nickel and selenium), mercury and hexavalent chromium. The scope of the existing data provided was the result of consensus reached by EPA, NAIMA and industry

representatives. In addition to the existing data submitted to EPA, extensive new emissions data is being collected from virtually all companies through the “BTEC, Inc. Quality Assurance Project Plan for the Mineral Wool and Wool Fiberglass Emissions Test Program.” This Test Program will collect and submit to EPA, through EPA’s Electronic Reporting Tool, representative emissions data for the following pollutants: formaldehyde, methanol, phenol, 

particulate matter, carbon monoxide, carbonyl sulfide, hydrogen fluoride, metals (antimony, arsenic, beryllium, 

cadmium, chromium, cobalt, lead, manganese, nickel and selenium), mercury and hexavalent chromium.
FORM F-1 

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

For each Process Unit:

 Process Unit ID Process Line IDII. Capital Costs Base year 7. Size of Company (approximate number of employees including all subsidiaries, branches, and related establishments owned):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) 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.

The company objects to this request because it serelevant to the EPA Administrator's review obligatioAct Section 112(d)(6) and 112(f)(2).
FORM F-1 

COST

The company objects to this request because it serelevant to the EPA Administrator's review obligatioAct Section 112(d)(6) and 112(f)(2).

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).

Wool fiberglass insulation comprises the major market for residential insulation material used in the United States. The remaining market consists of cellulose (scrap newspaper) treated to resist fires, spray foam, foam boards, cotton treated to resist fires, and wool treated to resist fires.Wool fiberglass insulation is preferred over these alternative insulation materials because it is easilyeconomically, and safety installed in various building settings, has superior fire performance capabilities, and a 70-year history of proven performance and durability.
FORM F-2

COSTI. Air Pollution Control Device (APCD) For each APCD: APCD ID Process Unit IDII. Capital Costs Base year  7. Size of Company (approximate number of employees including all subsidiaries, branches, and related establishments owned): 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 financining APCD Retrofit installation Field erected or modularIII. Annual Operating Costs Base year (most recent fiscal year) Maintenance materials and replacement parts (specify costs by item) Raw materials costs ($/yr) for each labor class (hr/hr) for each labor class Utilites (breackdown for each utility) Waste treatment and/or disposal

The company objects to this request because it serelevant to the EPA Administrator's review obligatioAct Section 112(d)(6) and 112(f)(2).
FORM F-2

 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. Alternatively, if company is publicly owned, you can provide your company's web link to this information.