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 300 Sunshine Rd. City Kansas City State Kansas Zip Code 66115 County Wyandotte Facility Coordinates Latitude (decimal degrees, six decimal places) 39.148578 Longitude (decimal degrees, six decimal places) 94.614942 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:

350

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

4

For each process line: Process Line 1 Process Line 2 Process Line 3  Process line identification names or numbers 70 K5 J6  Type of process line (e.g., rotary spin, flame attenuation) Rotary Spin Rotary Spin Rotary Spin  Maximum annual production rate (tons/yr) Age of process equipment (yrs) 35 25 36  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 material is mixed in batch house and pneumatically 

conveyed to furnace.

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.

 Total yearly consumption of binder (gal/yr) Cost of binder ($/gal) for most recent year (specify year) Are binder storage and mixing tanks vented to outside/inside? Binder mix and storage tanks are vented inside. 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

 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 70 Furnace (70FURNACE) 

(stack 01-03 and 01-04)

J5 Furnace (J5FURNACE) (stack 03-05)

 Process line(s) served (identification name/number) 70 J6 and U3 Latitude (decimal degrees, six decimal places) 39.1496769 (stack 01-03) and 

39.1495919 (stack 01-04)

39.1498394

 Longitude (decimal degrees, six decimal places) -94.6150889 (stack 01-03) and 

-94.6150906 (stack 01-04)

-94.6141128

 Stack or vent height (units) 67.11 ft (each) 67.57 ft. Stack or vent diameter (units) 4.00 ft. (each) 3.00 ft. Manufacturer and model Cold Top Oxy-Fuel Date of original installation 1975 1998 Estimate of remaining lifetime (yrs) N/A. Continued maintenance 

can maintain indefinite life.

N/A. Continued maintenance can maintain indefinite life.

 Major rebuilds: What constitutes a major rebuild 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
FORM B-3

PLANT OPERATIONSIII. Process - Glass Melting Furnace For each Glass Melting Furnace: 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) Stack or vent diameter (units) Manufacturer and model Date of original installation Estimate of remaining lifetime (yrs) 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

Furnace 3

K5 Furnace (K5FURNACE) (stack 03-25)K5 39.1496133-94.6141822101.2 ft.3.00 ft.Oxy-Fuel1998N/A. Continued maintenance can maintain indefinite life.N/AN/AN/AN/A
FORM B-3

PLANT OPERATIONSIII. Process - Glass Melting Furnace For each Glass Melting Furnace: Furnace 1 Furnace 2 Process unit identification name/number 70 Furnace (70FURNACE) 

(stack 01-03 and 01-04)

J5 Furnace (J5FURNACE) (stack 03-05)

 Process line(s) served (identification name/number) 70 J6 and U3 Increase or decrease in emissions N/A N/A Fuel type: electric, gas, or oil Electric Electric/Gas Fuel consumption rate (KW/ton of glass or Btu/ton of glass) List HAPs that are in refractory material Chromium Compounds Chromium Compounds 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) Nature and frequency of routine/preventive maintenance procedures

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.

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. 
FORM B-3

PLANT OPERATIONSIII. Process - Glass Melting Furnace For each Glass Melting Furnace: Process unit identification name/number Process line(s) served (identification name/number) Increase or decrease in emissions Fuel type: electric, gas, or oil  Fuel consumption rate (KW/ton of glass or Btu/ton of glass) List HAPs that are in refractory material 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) Nature and frequency of routine/preventive maintenance procedures

Furnace 3

K5 Furnace (K5FURNACE) 

(stack 03-25)K5 N/AGas/OxyChromium CompoundsDaily, 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. 
FORM B-3

PLANT OPERATIONSIII. Process - Glass Melting Furnace For each Glass Melting Furnace: Furnace 1 Furnace 2 Process unit identification name/number 70 Furnace (70FURNACE) 

(stack 01-03 and 01-04)

J5 Furnace (J5FURNACE) (stack 03-05)

 Process line(s) served (identification name/number) 70 J6 and U3 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. Batch wetting installed.

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-to-landfill, GHG, water consumption, VOC's, particulate matter, NOx and energy. DEP installed to meet MACT Subpart NNN requirements.

 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-3

PLANT OPERATIONSIII. Process - Glass Melting Furnace For each Glass Melting Furnace: Process unit identification name/number Process line(s) served (identification name/number) Describe process modification(s) since 1999 that reduce emissions Describe future source reduction plans and schedules

Furnace 3

K5 Furnace (K5FURNACE) 

(stack 03-25)K5 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-to-landfill, GHG, water consumption, VOC's, particulate matter, NOx and energy.None currently approved or scheduled at this time.
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 70 Forming (70FORMING) J6 Forming (J6FORMIN Process line(s) served (identification name/number) 70 J6 Latitude (decimal degrees, six decimal places) 39.1493044 (stack 01-07), 

39.1500183 (stack 01-08), 39.1494297 (stack 01-09) and 39.1494853 (stack 01-10)

39.1492742 (stack 04-139.1493311 (stack 04-139.1494586 (stack 04-139.1494919 (stack 04-1

 Longitude (decimal degrees, six decimal places) -94.6147317 (stack 01-07), -

94.6147239 (stack 01-08), -94.6148525 (stack 01-09) and -94.6149111 (stack 01-10)

-94.6138611 (stack 04-194.6141175 (stack 04-194.6141147 (stack 04-194.6141353 (stack 04-1

 Stack or vent height (units) 93.40 ft. (stack 01-07), 100.75 

ft. (stack 01-08), 99.40 ft. (stack 01-09) and 93.40 ft. (stack 01-10)

79.18 ft. (stack 04-11), 1ft. (stack 04-12), 92.35 f04-14) and 88.98 ft. (sta16)

 Stack or vent diameter (units) 4.33 ft. (stack 01-07), 4.58 ft. 

(stack 01-08), 4.00 ft. (stack 01-09) and 4.33 ft. (stack 01-10)

3.42 ft. (stack 04-11), 4.(stack 04-12), 3.75 ft. (s14) and 3.422 ft. (stack 

 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:
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) Stack or vent diameter (units) 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:

Forming Operation 3 Forming Operation 

K5 Forming (K5FORMINGN and K5FORMINGS)

N/A. Unbonded Loose F(ULF FORMING) is not spin / flame attenuation.

K5 N/A39.1492742 (stack 04-11), 39.1493311 (stack 04-12), 39.1494586 (stack 04-14) and 39.1494919 (stack 04-16)

N/A

-94.6138611 (stack 04-11), -94.6141175 (stack 04-12), -94.6141147 (stack 04-14) and -94.6141353 (stack 04-16)

N/A

79.18 ft (stack 04-11), 100.75 ft. (stack 04-12), 92.35 ft. (stack 04-14) and 88.98 ft. (stack 04-16)

N/A

3.42 ft. (stack 04-11), 4.58 ft. (stack 04-12), 3.75 ft. (stack 04-14) and 3.42 ft. (stack 04-16)

N/AN/A

Air and Flame N/AYes N/A
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 70 Forming (70FORMING) J6 Forming (J6FORMIN Process line(s) served (identification name/number) 70 J6 What constitutes a major rebuild The company undertakes 

routine repair and replacement projects. As with the furnace, these projects are normally “asis” maintenance projects that do 

not impact the forming emissions. Therefore, the company does not consider these to be major rebuilds for the purpose of this ICR.

The company undertakeroutine repair and replacprojects. As with the furthese projects are norm

is” maintenance projects not impact the forming emissions. Therefore, tcompany does not consthese to be major rebuildthe 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) Binder applied and application rate (gpm) Other material applied and application rate (gpm) None None 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.
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) 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) Binder applied and application rate (gpm) Other material applied and application rate (gpm) 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

Forming Operation 3 Forming Operation 

K5 Forming (K5FORMINGN and K5FORMINGS)

N/A. Unbonded Loose F(ULF FORMING) is not spin / flame attenuation.

K5 N/AThe company undertakes routine repair and replacement projects. As with the furnace, these projects are normally “asis” maintenance projects that do not impact the forming emissions. Therefore, the company does not consider these to be major rebuilds for the purpose of this ICR.

N/A

N/A N/AN/A N/AN/A N/AN/A N/AN/A N/A

N/AN/AN/A

None N/A

N/AN/A

Compressed air lapping system N/A1"-6" as formed, up to 15" on ramp.

N/AN/A

None recirculated, 100% exhausted.

N/A
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 70 Forming (70FORMING) J6 Forming (J6FORMIN Process line(s) served (identification name/number) 70 J6 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
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) Nature and frequency of routine/preventive maintenance procedures

Forming Operation 3 Forming Operation 

K5 Forming (K5FORMINGN and K5FORMINGS)

N/A. Unbonded Loose F(ULF FORMING) is not spin / flame attenuation.

K5 N/AGeneral 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.

N/A
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 70 Forming (70FORMING) J6 Forming (J6FORMIN Process line(s) served (identification name/number) 70 J6 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) Describe process modification(s) since 1999 that reduce emissions Describe future source reduction plans and schedules

Forming Operation 3 Forming Operation 

K5 Forming (K5FORMINGN and K5FORMINGS)

N/A. Unbonded Loose F(ULF FORMING) is not spin / flame attenuation.

K5 N/A

N/A

None currently approved or 

scheduled at this time.

N/A
FORM B-5

PLANT OPERATIONSV. Process - Curing  For each Curing Oven: Curing Oven 1 Curing Oven 2 Process unit identification name/number 70 Curing (70OVEN) K5 Curing (K5OVEN) Process line(s) served (identification name/number) 70 K5  Latitude (decimal degrees, six decimal places) 39.1494136 (charge) and 

39.1491536 (discharge)

39.1490925 (charge) and 39.1487989 (discharge)

 Longitude (decimal degrees, six decimal places) -94.6149364 (charge) and -

94.6147897 (discharge)

-94.6138017 (charge) and -94.6138078 (discharge)

 Stack or vent height (units) 42.27 ft. (charge) and 37.84 ft. 

(discharge)

40.50 ft. (charge) and 45.00 ft. (discharge)

 Stack or vent diameter (units) 1.66 ft. (charge) and 2.0 ft. 

(discharge)

2.5 ft. (each) and 1.83 ft. (discharge)

 Method of curing  Manufacturer and model OC Proprietary Design OC Proprietary Design Date of original installation 1975 1985 Major rebuilds: What constitues 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)
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) Stack or vent diameter (units) Method of curing  Manufacturer and model Date of original installation Major rebuilds: What constitues 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)

Curing Oven 3 Curing Oven 4

J6 Curing (J6OVEN) N/A - U3 line (unbonded loose 

fill) does not have curing.

J6 N/A-94.6140550 (charge) and -94.6141042 (discharge)

N/A

39.1492933 (charge) and 

39.1491664 (discharge)

N/A

48.50 ft. (charge) and 35.58 ft. 

(discharge)

N/A

1.6 ft. (each) N/A

N/A

OC Proprietary Design N/A1985 N/AThe 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/A

N/A N/AN/A N/AN/A N/AN/A N/AN/A N/ANatural Gas N/A

N/A
FORM B-5

PLANT OPERATIONSV. Process - Curing  For each Curing Oven: Curing Oven 1 Curing Oven 2 Process unit identification name/number 70 Curing (70OVEN) K5 Curing (K5OVEN) Process line(s) served (identification name/number) 70 K5  Moisture content wt (%) of formed mat:  inlet 2.5 - 5% 2.5 - 5% outlet <0.5% <0.5% Air flow rate (acfm @ °F) from curing 19,000 acfm @ 130 °F 20,200 acfm @ 145 °F Exhaust air temperature (°F) 130 °F 145 °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.
FORM B-5

PLANT OPERATIONSV. Process - Curing  For each Curing Oven: Process unit identification name/number Process line(s) served (identification name/number) Moisture content wt (%) of formed mat:  inlet outlet 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

Curing Oven 3 Curing Oven 4

J6 Curing (J6OVEN) N/A - U3 line (unbonded loose 

fill) does not have curing.

J6 N/A2.5 - 5% N/A<0.5% N/A21,200 acfm @ 140 °F N/A140 °F N/A

N/AN/A

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.

N/A
FORM B-5

PLANT OPERATIONSV. Process - Curing  For each Curing Oven: Curing Oven 1 Curing Oven 2 Process unit identification name/number 70 Curing (70OVEN) K5 Curing (K5OVEN) Process line(s) served (identification name/number) 70 K5  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) Describe process modification(s) since 1999 that reduce emissions Describe future source reduction plans and schedules

Curing Oven 3 Curing Oven 4

J6 Curing (J6OVEN) N/A - U3 line (unbonded loose 

fill) does not have curing.

J6 N/A

N/A

None currently approved or 

scheduled at this time.

N/A
FORM B-6

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

 Process unit identification name/number 70 Cooling (70COOLING) K5 Cooling (K5COOLING) J6 Co

 Process line(s) served (identification name/number) 70 K5 J6 Latitude (decimal degrees, six decimal places) 39.1490225 (stack 17-08) and 

39.1488675 (stack 17-12)

39.1486992 (07-16) and 39.1486250 (07-17)

39.1439.14

 Longitude (decimal degrees, six decimal places) -94.6150164 (stack 17-08) and 

-94.6151325 (stack 17-12)

-94.6139772 (07-16) and -94.6139789 (07-17)

-94.6-94.6

 Stack or vent height (units) 33.39 ft.(stack 17-08) and 

35.42 ft. (stack 17-12)

34 ft. (07-16) and 33 ft. (07-17) 42.30 

and 3

south

 Stack or vent diameter (units) 2.08 ft. (stack 17-08) and 1.65 

ft. (stack 17-12)

3.0 ft. (each) 3.08 

 Cooling air flow rate (acfm @ °F) 38,400 acfm @ 77 °F 35,860 acfm @ 90 °F 36,70

 Percentage of cooling air recirculated (if any) None None None  Cooling air temperature (°F) 70 - 120 °F 85 - 120 °F 70 - 1
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) Stack or vent diameter (units) Cooling air flow rate (acfm @ °F) 

 Percentage of cooling air recirculated (if any) Cooling air temperature (°F)

Cooling Operation 4

N/A - U3 line (unbonded loose fill) does not have cooling.N/AN/AN/AN/AN/AN/AN/AN/A
FORM B-6

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

 Process unit identification name/number 70 Cooling (70COOLING) K5 Cooling (K5COOLING) J6 Co

 Process line(s) served (identification name/number) 70 K5 J6

 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.

Genefollow that imainRepaperfodurindowncleanweeksuch replatrack occurepla

 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.

None sched
FORM B-6

PLANT OPERATIONSVI. Process - Cooling For each Cooling Operation: Process unit identification name/number Process line(s) served (identification name/number) Nature and frequency of routine/preventive maintenance procedures Describe process modification(s) since 1999 that reduce emissions Describe future source reduction plans and schedules

Cooling Operation 4

N/A - U3 line (unbonded loose fill) does not have cooling.N/A

N/AN/AN/A
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 ESP 2 Process line(s) (identification name/number) 70 J5  Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan)

70 Forming with WEP (70FORMING and 70WEPB) 

(stack 01-08)

J5 Furnace with DEP (J5FURNACE and J5D(stack 03-01)

 Latitude (decimal degrees, six decimal places) 39.1500183 39.1496172 Longitude (decimal degrees, six decimal places) -94.6147239 -94.6142747 Stack or vent height (units) 100.75 ft. 92.92 ft. Stack or vent diameter (units) 4.58 ft. 3 ft. Manufacturer and model Alstom Power FAV 15 15 3OH Alstom Power 3x45f-35 Date of original installation 1998 1998 Number of collection plates and configuration 38,38,76/Field 90/field,  Gas flow rate to ESP (acfm @ °F) 41,080 acfm @ 101 °F 26,733 acfm @ 484 °F  Inlet gas temperature (°F) 101 °F 484 °F  Outlet gas temperature (°F) 99 °F 462 °F  Inlet grain loading (gr/dscf) 0.0228 gr/dscf 0.2582 gr/dscf Outlet grain loading (gr/dscf) 0.0010 gr/dscf 0.0020 gr/dscf Average stack opacity (%) <20% <20% Pressure drop across ESP (in. H2O gauge) 1" 3" Plate area (ft2) 15,501 16,276 Vendor guarantee on ESP efficiency (attach copy) Yes. Provided on CD. Yes. Provided on CD. Method of plate cleaning and frequency Water. Continuously flows. Rappers. Cleaning bas

monitoring parameters

 Flow rate of plate wash water to ESP (gpm), if applicable 200 - 300 gpm N/A Temperature of plate wash water to ESP (°F), if applicable 100 °F N/A Source of plate wash water used for cleaning, if applicable Recirculation N/A Concentration (mg/l) of dissolved and suspended solids in plate wash water, if applicable

0.09 - 0.314 N/A

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

applicable

None None

 Amount of wastewater generated (gpd), if applicable 7,200 gpd blow down to sewer 7,200 gpd blow down to 

 Amount of wastewater recycled (gpd), if applicable None None
FORM C-1

AIR POLLUTION CONTROLI. Electrostatic Precipitator (ESP) For each ESP: 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. H2O gauge) Plate area (ft2) 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

ESP 3 ESP 4

J6 K5 J6 Forming with WEP (J6FORMING and J6WEPB) (stack 04-18)

K5 Furnace with DEP (K5FURNACE and K5D(stack 03-25)

39.1500172 39.1498394-94.6146356 -94.6141128100.75 ft. 101.2 ft.4.58 ft. 3 ft.Alstom Power FAV 15 15 3OH Alstom Power 3x45f-351998 199838,38,76/Field 90/field, 31,207 acfm @ 100 °F 27,538 acfm @ 457 °F 100 °F 484 °F 99 °F 457 °F 0.0142 gr/dscf 0.8337 gr/dscf0.0011 gr/dscf 0.0164 gr/dscf<20% <20%1" 3"15,501 16,276Yes. Provided on CD. Yes. Provided on CD.Water. Continuously flows. Rappers. Cleaning bas

monitoring parameters

200 - 300 gpm N/A100 °F N/ARecirculation N/A0.09 - 0.314 N/ANone None7,200 gpd blow down to sewer 7,200 gpd blow down to None None
FORM C-1

AIR POLLUTION CONTROLI. Electrostatic Precipitator (ESP) For each ESP: 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. H2O gauge) Plate area (ft2) 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

ESP 5 ESP 6

K5 K5 K5 Forming with WEP (K5FORMING and K5WEPC) (stack 04-13)

K5 Forming with WEP (K5FORMING and K5W(stack 04-15)

39.1500150 39.1500161-94.6144594 -94.6145475100.75 ft. 80.85 ft.4.58 ft. 4.58 ft.Alstom Power FAV 15 15 3OH Alstom Power FAV 15 1998 199838,38,76/Field 38,38,76/Field36,620 acfm @ 91 °F 32,633 acfm @ 93 °F 91 °F 93 °F 98 °F 98 °F 0.0191 gr/dscf 0.0177 gr/dscf0.0001 gr/dscf 0.0013 gr/dscf<20% <20%1" 1"15,501 15,501Yes. Provided on CD. Yes. Provided on CD.Water. Flush system. Water. Flush system.200 - 300 gpm 200 - 300 gpm100 °F 100 °FRecirculation Recirculation0.09 - 0.314 0.09 - 0.314None None7,200 gpd blow down to sewer 7,200 gpd blow down to None None
FORM C-1

AIR POLLUTION CONTROLI. Electrostatic Precipitator (ESP) For each ESP: ESP 1 ESP 2 Process line(s) (identification name/number) 70 J5  Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan)

70 Forming with WEP (70FORMING and 70WEPB) 

(stack 01-08)

J5 Furnace with DEP (J5FURNACE and J5D(stack 03-01)

 Amount of wastewater disposed of (gpd), if applicable 7,200 gpd blow down to sewer 7,200 gpd blow down to  Method of wastewater disposal, if applicable City sewer system City sewer system Quantity of solid waste collected (lbs/yr) 0 lbs 1,000 - 1,500 lbs. Sma

quantities of DEP residbecomes contaminated process and must be d

 Quantity of solid waste recycled (lbs/yr) 0 lbs 0 lbs Quantity of solid waste disposed of (lbs/yr) 0 lbs 1,000 - 1,500 lbs Method of solid waste disposal N/A Hazardous Waste Land 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.

General maintenance afollow a prescribed schthat is detailed in the maintenance tracking sSystems are continuoumonitored and notificat

occur that initiate maintSIR repair and replacemconducted as needed. Electrode replacement 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 malfunctions / repaired; and mechanical malfunctions / repaired.

As reported in Title V d

reports: electrical malfurepaired; and mechanicmalfunctions / repaired
FORM C-1

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

ESP 3 ESP 4

J6 K5 J6 Forming with WEP (J6FORMING and J6WEPB) (stack 04-18)

K5 Furnace with DEP (K5FURNACE and K5D(stack 03-25)

7,200 gpd blow down to sewer 7,200 gpd blow down to City sewer system City sewer system0 lbs 1,000 - 1,500 lbs. Sma

quantities of DEP residbecomes contaminated process and must be d

0 lbs 0 lbs0 lbs 1,000 - 1,500 lbsN/A Hazardous Waste LandGeneral 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.

General maintenance afollow a prescribed schthat is detailed in the maintenance tracking sSystems are continuoumonitored and notificat

occur that initiate maintSIR repair and replacemconducted as needed. Electrode replacement on a a12-15 year cycle

As reported in Title V deviation 

reports: electrical malfunctions / repaired; and restricted water flow / repair.

As reported in Title V d

reports: electrical malfurepaired; and mechanicmalfunctions / repaired
FORM C-1

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

ESP 5 ESP 6

K5 K5 K5 Forming with WEP (K5FORMING and K5WEPC) (stack 04-13)

K5 Forming with WEP (K5FORMING and K5W(stack 04-15)

7,200 gpd blow down to sewer 7,200 gpd blow down to City sewer system City sewer system0 lbs 0 lbs0 lbs 0 lbs0 lbs 0 lbsN/A N/AGeneral 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.

General maintenance afollow a prescribed schthat is detailed in the maintenance tracking sSystems are continuoumonitored and notificat

occur that initiate maintSIR repair and replacemconducted as needed. Electrode replacement on a a12-15 year cycle

As reported in Title V deviation 

reports: electrical malfunctions / repaired; mechanical malfunctions / repaired; and restricted water flow / repair.

As reported in Title V d

reports: electrical malfurepaired; mechanical malfunctions / repairedrestricted water flow / re
FORM C-1

AIR POLLUTION CONTROLI. Electrostatic Precipitator (ESP) For each ESP: ESP 1 ESP 2 Process line(s) (identification name/number) 70 J5  Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan)

70 Forming with WEP (70FORMING and 70WEPB) 

(stack 01-08)

J5 Furnace with DEP (J5FURNACE and J5D(stack 03-01)

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

Secondary voltage and amperage of 3rd field.

Secondary voltage and amperage of 3rd field.

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

scheduled at this time.

None currently approvescheduled at this time.
FORM C-1

AIR POLLUTION CONTROLI. Electrostatic Precipitator (ESP) For each ESP: Process line(s) (identification name/number) Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan) Continuous monitoring method(s) used to monitor ESP performance, including parameters monitored Describe any plans to replace or upgrade ESP

ESP 3 ESP 4

J6 K5 J6 Forming with WEP (J6FORMING and J6WEPB) (stack 04-18)

K5 Furnace with DEP (K5FURNACE and K5D(stack 03-25)

Secondary voltage and amperage of 3rd field.

Secondary voltage and amperage of 3rd field.

None currently approved or scheduled at this time.

None currently approvescheduled at this time.
FORM C-1

AIR POLLUTION CONTROLI. Electrostatic Precipitator (ESP) For each ESP: Process line(s) (identification name/number) Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan) Continuous monitoring method(s) used to monitor ESP performance, including parameters monitored Describe any plans to replace or upgrade ESP

ESP 5 ESP 6

K5 K5 K5 Forming with WEP (K5FORMING and K5WEPC) (stack 04-13)

K5 Forming with WEP (K5FORMING and K5W(stack 04-15)

Secondary voltage and amperage of 3rd field.

Secondary voltage and amperage of 3rd field.

None currently approved or scheduled at this time.

None currently approvescheduled at this time.
FORM C-2

AIR POLLUTION CONTROLII. Scrubber For each Scrubber: Scrubber 1 Scrubber 2  Process line(s) (identification name/number) 70 70  Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan)

70 Cooling (70COOLING and 70SCRUBBER001) (Stack 17-08)

70 Cooling (70COOLING and 70SCRUBBER002) (Stack 17-12)

 Latitude (decimal degrees, six decimal places) 39.1490225 (stack 17-08) 39.1488675 (stack 17-12)  Longitude (decimal degrees, six decimal places) -94.6150164 (stack 17-08) -94.6151325 (stack 17-12) 

 Stack or vent height (units) 33.39 ft. 35.52 ft.  Stack or vent diameter (units) 2.08 ft. 1.67 ft.  Manufacturer and model Monroe Environmental Monroe Environmental  Date of original installation 1975 1975  Type (e.g., venturi, orifice) Venturi Venturi  Gas flow rate to scrubber (acfm @ °F) 29,000 acfm @ 72 °F 9,426 acfm @ 76 °F 

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

 Outlet gas temperature (°F) 80 - 120 °F 80 - 120 °F 

 Inlet grain loading (gr/dscf) No data available. No data available.  Outlet grain loading (gr/dscf) No data available. No data available.  Average stack opacity (%) <20% <20%  Water flow rate to scrubber (gpm) 200 - 500 gpm 200 - 500 gpm  Percent of scrubber water from recycled wastewater 100% 100% 

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

Industrial Reclaim Clear Water System. No 

pretreatment.

Industrial Reclaim Clear Water System. No pretreatment.

 HAP composition of wastewater (mg/L) 100 - 150 mg/L 100 - 150 mg/L  Concentration (mg/L) of dissolved and suspended solids in scrubbing water

No data available. No data available. 

 Scrubbing water temperature (°F) 80 - 110 °F 80 - 110 °F 

 Liquid/gas ratio (gal/103 acfm) No data available. No data available. 
FORM C-2

AIR POLLUTION CONTROLII. Scrubber For each Scrubber: 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)

Scrubber 4 Scrubber 5 

K5 J6 K5 Cooling (K5COOLING and K5SCRUBBER002) (Stack 07-17)

J6 Cooling (J6COOLING and J6SCRUBBER001) (Stack 08-12)

39.1486250 (stack 07-17) 39.1489569 (stack 08-12) 

-94.6139789 (stack 07-17) -94.6140953 (stack 08-12) 

33 ft. 42.3 ft. 3 ft. 3.25 ft. x 3.08 ft. 

(rectangular)

Monroe Environmental Monroe Environmental 1985 1994 Venturi Venturi 15,957 acfm @ 90 °F 36,694 acfm @ 75 °F 100 - 120 °F 100 - 120 °F 80 - 120 °F 80 - 120 °F No data available. No data available. 0.0028 gr/dscf No data available. <20% <20% 450 - 500 gpm 337 - 631 gpm 100% 100% Industrial Reclaim Clear Water System. No 

pretreatment.

Industrial Reclaim Clear Water System. No pretreatment.

100 - 150 mg/L 100 - 150 mg/L No data available. No data available. 80 - 110 °F 80 - 110 °F No data available. No data available. 
FORM C-2

AIR POLLUTION CONTROLII. Scrubber For each Scrubber: Scrubber 1 Scrubber 2  Process line(s) (identification name/number) 70 70  Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan)

70 Cooling (70COOLING and 70SCRUBBER001) (Stack 17-08)

70 Cooling (70COOLING and 70SCRUBBER002) (Stack 17-12)

 Pressure drop across scrubber (in. H2O gauge) 4 - 12" 4 - 12" 

 Amount of wastewater generated (gpd) 0 gpd (infrequent 

discharges)

0 gpd (infrequent discharges)

 Amount of wastewater recycled (gpd) 100% 100%  Amount of wastewater disposed of (gpd) 0 gpd (infrequent 

discharges)

0 gpd (infrequent discharges)

 Method of wastewater disposal N/A N/A  Quantity of solid waste collected (lbs/yr) 220,000 - 300,000 lbs (all 

sources - wash water 

system)

220,000 - 300,000 lbs (all sources - wash water system)

 Quantity of solid waste recycled (lbs/yr) 0 lbs 0 lbs  Quantity of solid waste disposed of (lbs/yr) 220,000 - 300,000 lbs (all 

sources - wash water 

system)

220,000 - 300,000 lbs (all sources - wash water system)

 Method of solid waste disposal Local Solid Waste Landfill Local Solid Waste Landfill  Vendor guarantee on scrubber efficiency (attach copy) None provided. None provided. 
FORM C-2

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

Scrubber 4 Scrubber 5 

K5 J6 K5 Cooling (K5COOLING and K5SCRUBBER002) (Stack 07-17)

J6 Cooling (J6COOLING and J6SCRUBBER001) (Stack 08-12)

4 - 12" 4 - 12" 0 gpd 0 gpd 100% 100% 0 gpd 0 gpd N/A N/A 220,000 - 300,000 lbs (all sources - wash water system)

220,000 - 300,000 lbs (all sources - wash water system)

0 lbs 0 lbs 220,000 - 300,000 lbs (all sources - wash water system)

220,000 - 300,000 lbs (all sources - wash water system)

Local Solid Waste Landfill Local Solid Waste Landfill None provided. None provided. 
FORM C-2

AIR POLLUTION CONTROLII. Scrubber For each Scrubber: Scrubber 1 Scrubber 2  Process line(s) (identification name/number) 70 70  Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan)

70 Cooling (70COOLING and 70SCRUBBER001) (Stack 17-08)

70 Cooling (70COOLING and 70SCRUBBER002) (Stack 17-12)

 Nature and frequency of preventive maintenance procedures 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.

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.

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

As reported in Title V deviation reports: equipment failure / 

repaired.

As reported in Title V deviation reports: equipment failure / repaired.

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

water flow (gpm) & differential pressure.

water flow (gpm) & differential pressure.

 Plans to replace or upgrade scrubber None currently approved 

or scheduled at this time.

None currently approved or scheduled at this time.
FORM C-2

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

Scrubber 4 Scrubber 5 

K5 J6 K5 Cooling (K5COOLING and K5SCRUBBER002) (Stack 07-17)

J6 Cooling (J6COOLING and J6SCRUBBER001) (Stack 08-12)

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.

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.

As reported in Title V deviation reports: equipment failure / 

repaired.

As reported in Title V deviation reports: restricted water flow / repaired.

water flow (gpm) & differential pressure.

water flow (gpm) & differential pressure.

None currently approved or scheduled at this time.

None currently approved or scheduled at this time.
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) J6 K5 70 Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan)

J5 Batch (J5 BATCH, CEJ5DC001) (stack 03-02) K5 Batch (K5 BATCH, CE- K5DC001) (stack 03-26) 70 Batc

70DC00

 Latitude (decimal degrees, six decimal places) 39.1496028 39.1496822 39.1497 Longitude (decimal degrees, six decimal places) -94.6143314 -94.6139181 -94.615 Stack or vent height (units) 61.67 ft. 62.83 ft. 10.08 ft Stack or vent diameter (units) 0.83 ft. 0.83 ft. 0.92 ft. Manufacturer and model Flex Kleen Farr Flex Kle Date of original installation 2006 2008 2007 Number of compartments 1 1 1 Number of bags per compartment 36 6 49 Filter material and coatings applied Polyester media No data available. Polyeste Fabric weight (oz/yd2) 8 No data available. 8 oz/yd2

 Filter surface area (ft2) 720 ft2 No data available. 980 ft2

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

 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) <0.02 gr/dscf <0.02 gr/dscf <0.02 g Average stack opacity (%) <20% <20% <20% Overall pressure drop (in. H2O gauge) No data available. No data available. No data 

 Method and frequency of bag cleaning No data available. No data available. No data  Vendor guarantee on fabric filter efficiency (attach 

copy)

None provided. None provided. None pr
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) Stack or vent diameter (units) 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) Average stack opacity (%) Overall pressure drop (in. H2O gauge)

 Method and frequency of bag cleaning Vendor guarantee on fabric filter efficiency (attach 

copy)

Fabric Filter 4 Fabric Filter 5 

J6, K5 and 70 J6, K5 and 70 J6, K5 aRaw Material Storage Bin #1 (BATCHHOUSE1, CEDCRMBIN1) (stack B-01)

Raw Material Storage Bin #2A (BATCHHOUSE2A, CEDCRMBIN2A) (stack B-02)

Raw Ma#2B (BADCRMB

39.1491731 39.1491839 39.1492-94.6135106 -94.6135103 -94.61344.5 ft. 44.5 ft. 44.5 ft.0.61 ft. 0.61 ft. 0.61 ft.Manufacturer not known. Model No. 96AVS16, Style #2

Manufacturer not known. Model No. 96AVS16, Style #2

ManufacModel N#2

2008 2008 20081 1 116 16 16Polypro Polypro Polypro16 oz/yd2 16 oz/yd2 16 oz/yd76.25 ft2 76.25 ft2 76.25 ft2No data available. No data available. No data Ambient Ambient AmbienAmbient Ambient AmbienNo data available. No data available. No data <0.02 gr/dscf <0.02 gr/dscf <0.02 g<20% <20% <20%No data available. No data available. No data No data available. No data available. No data None provided. None provided. None pr
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) Stack or vent diameter (units) 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) Average stack opacity (%) Overall pressure drop (in. H2O gauge)

 Method and frequency of bag cleaning Vendor guarantee on fabric filter efficiency (attach 

copy)

Fabric Filter 7 Fabric Filter 8 

J6, K5 and 70 J6, K5 and 70 J6, K5 aRaw Material Storage Bin #3 (BATCHHOUSE3, CEDCRMBIN3) (stack B-04)

Raw Material Storage Bin #4 (BATCHHOUSE4, CEDCRMBIN4) (stack B-05)

Raw Ma#5A (BADCRMB

39.1492361 39.1492883 39.1493-94.6135089 -94.6135072 -94.61344.5 ft. 44.5 ft. 44.5 ft.0.61 ft. 0.61 ft. 0.61 ft.Manufacturer not known. Model No. 96AVS16, Style #2

Manufacturer not known. Model No. 96AVS16, Style #2

ManufacModel N#2

2008 20208 20081 1 116 16 16Polypro Polypro Polypro16 oz/yd2 16 oz/yd2 16 oz/yd76.25 ft2 76.25 ft2 76.25 ft2No data available. No data available. No data Ambient Ambient AmbienAmbient Ambient AmbienNo data available. No data available. No data <0.02 gr/dscf <0.02 gr/dscf <0.02 g<20% <20% <20%No data available. No data available. No data No data available. No data available. No data None provided. None provided. None pr
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) Stack or vent diameter (units) 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) Average stack opacity (%) Overall pressure drop (in. H2O gauge)

 Method and frequency of bag cleaning Vendor guarantee on fabric filter efficiency (attach 

copy)

Fabric Filter 10 Fabric Filter 11 F

J6, K5 and 70 J6, K5 and 70 J6, K5 aRaw Material Storage Bin #5B (BATCHHOUSE5B, CEDCRMBIN5B) (stack B-07)

Raw Material Storage Bin #6 (BATCHHOUSE6, CEDCRMBIN6) (stack B-08)

Raw Ma#7A (BADCRMB

39.1493403 39.1494364 39.1494-94.6135058 -94.6135031 -94.61344.5 ft. 44.5 ft. 44.5 ft.0.61 ft. 0.61 ft. 0.61 ft.Manufacturer not known. Model No. 96AVS16, Style #2

Manufacturer not known. Model No. 96AVS16, Style #2

ManufacModel N#2

2008 2008 20081 1 116 16 16Polypro Polypro Polypro16 oz/yd2 16 oz/yd2 16 oz/yd76.25 ft2 76.25 ft2 76.25 ft2No data available. No data available. No data Ambient Ambient AmbienAmbient Ambient AmbienNo data available. No data available. No data <0.02 gr/dscf <0.02 gr/dscf <0.02 g<20% <20% <20%No data available. No data available. No data No data available. No data available. No data None provided. None provided. None pr
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) Stack or vent diameter (units) 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) Average stack opacity (%) Overall pressure drop (in. H2O gauge)

 Method and frequency of bag cleaning Vendor guarantee on fabric filter efficiency (attach 

copy)

Fabric Filter 13 Fabric Filter 14 F

J6, K5 and 70 J6, K5 and 70 J6, K5 aRaw Material Storage Bin #7B (BATCHHOUSE7B) (stack B-10)

Raw Material Storage Bin #8 (BATCHHOUSE8) (stack B11)

Raw Ma(BATCHDCRMB

39.1494886 (stack B-10) 39.1494969 (stack B-11) 39.1492-94.6135017 (stack B-10) -94.6135014 (stack B-11) -94.61344.5 ft. 44.5 ft. 44.5 ft.0.61 ft. 0.61 ft. 0.61 ft.Manufacturer not known. Model No. 96AVS16, Style #2

Manufacturer not known. Model No. 96AVS16, Style #2

ManufacModel N#2

20008 2008 20081 1 116 16 16Polypro Polypro Polypro16 oz/yd2 16 oz/yd2 16 oz/yd76.25 ft2 76.25 ft2 76.25 ft2No data available. No data available. No data Ambient Ambient AmbienAmbient Ambient AmbienNo data available. No data available. No data <0.02 gr/dscf <0.02 gr/dscf <0.02 g<20% <20% <20%No data available. No data available. No data No data available. No data available. No data None provided. None provided. None pr
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) Stack or vent diameter (units) 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) Average stack opacity (%) Overall pressure drop (in. H2O gauge)

 Method and frequency of bag cleaning Vendor guarantee on fabric filter efficiency (attach 

copy)

Fabric Filter 16 Fabric Filter 17 F

J6, K5 and 70 J6, K5 and 70 J6, K5 aRaw Material West Unloading (BATCHHOUSEUL, CEDCRUNLOAD) (stack B-20)

Raw Material East Unloading (stack B-24)

Raw Ma(BATCHDCBHM

39.1495447 (stack B-20) 39.1492394 39.1492-94.6135 (stack B-20) -94.6133892 -94.61333.5 ft. 0.08 ft. 9.50 ft.1 ft. 12.92 ft. 1.0 ft.Tech Air - SZ85-10-1334 (Serial No. 11-93-9248)

Flex Kleen 43/54-PSBL121(IIIG) No data 

2008 2008 20081 1 185 No data available. 40Polyester No data available. No data 16 oz/yd2 No data available. 16 oz/yd405 ft2 5,203 ft2 190 ft2No data available. No data available. No data Ambient Ambient AmbienAmbient Ambient AmbienNo data available. No data available. No data <0.02 gr/dscf <0.02 gr/dscf <0.02 g<20% <20% <20%No data available. 20" No data No data available. Manual. No frequency. No data None provided. None provided. None pr
FORM C-4

AIR POLLUTION CONTROLIV. Fabric Filter  For each Fabric Filter: Fabric Filter 1 Fabric Filter 2  Process line(s) (identification name/number) J6 K5 70 Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan)

J5 Batch (J5 BATCH, CEJ5DC001) (stack 03-02) K5 Batch (K5 BATCH, CE- K5DC001) (stack 03-26) 70 Batc

70DC00

 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) 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 

J6, K5 and 70 J6, K5 and 70 J6, K5 aRaw Material Storage Bin #1 (BATCHHOUSE1, CEDCRMBIN1) (stack B-01)

Raw Material Storage Bin #2A (BATCHHOUSE2A, CEDCRMBIN2A) (stack B-02)

Raw Ma#2B (BADCRMB

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

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

N/A (Clocollecte

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

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

N/A (Clocollecte

0 lbs 0 lbs 0 lbsN/A N/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.

Generaas needinspectipressurperformcartridge perform

None reported in Title V deviation reports. 

None reported in Title V deviation reports. 

None redeviatio

N/A N/A N/ANone 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) 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 7 Fabric Filter 8 

J6, K5 and 70 J6, K5 and 70 J6, K5 aRaw Material Storage Bin #3 (BATCHHOUSE3, CEDCRMBIN3) (stack B-04)

Raw Material Storage Bin #4 (BATCHHOUSE4, CEDCRMBIN4) (stack B-05)

Raw Ma#5A (BADCRMB

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

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

N/A (Clocollecte

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

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

N/A (Clocollecte

0 lbs 0 lbs 0 lbsN/A N/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.

Generaas needinspectipressurperformcartridge perform

None reported in Title V deviation reports. 

None reported in Title V deviation reports. 

None redeviatio

N/A N/A N/ANone 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) 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 10 Fabric Filter 11 F

J6, K5 and 70 J6, K5 and 70 J6, K5 aRaw Material Storage Bin #5B (BATCHHOUSE5B, CEDCRMBIN5B) (stack B-07)

Raw Material Storage Bin #6 (BATCHHOUSE6, CEDCRMBIN6) (stack B-08)

Raw Ma#7A (BADCRMB

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

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

N/A (Clocollecte

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

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

N/A (Clocollecte

0 lbs 0 lbs 0 lbsN/A N/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.

Generaas needinspectipressurperformcartridge perform

None reported in Title V deviation reports. 

None reported in Title V deviation reports. 

None redeviatio

N/A N/A N/ANone 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) 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 13 Fabric Filter 14 F

J6, K5 and 70 J6, K5 and 70 J6, K5 aRaw Material Storage Bin #7B (BATCHHOUSE7B) (stack B-10)

Raw Material Storage Bin #8 (BATCHHOUSE8) (stack B11)

Raw Ma(BATCHDCRMB

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

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

N/A (Clocollecte

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

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

N/A (Clocollecte

0 lbs 0 lbs 0 lbsN/A N/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.

Generaas needinspectipressurperformcartridge perform

None reported in Title V deviation reports. 

None reported in Title V deviation reports. 

None redeviatio

N/A N/A N/ANone 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) 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 16 Fabric Filter 17 F

J6, K5 and 70 J6, K5 and 70 J6, K5 aRaw Material West Unloading (BATCHHOUSEUL, CEDCRUNLOAD) (stack B-20)

Raw Material East Unloading (stack B-24)

Raw Ma(BATCHDCBHM

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

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

N/A (Clocollecte

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

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

N/A (Clocollecte

0 lbs 0 lbs 0 lbsN/A N/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.

Generaas needinspectipressurperformcartridge perform

None reported in Title V deviation reports. 

None reported in Title V deviation reports. 

None redeviatio

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

None currently approved or scheduled at this time.

None cuschedul
FORM C-5

AIR POLLUTION CONTROL Not applicable to this facility.V. Thermal Incinerator For each Thermal Incinerator: Thermal Incinerator 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 Fuel type: gas or oil N/A Fuel consumption rate (BTU/hr) N/A Inlet gas flow rate (acfm @ °F) N/A

 Inlet gas temperature (°F) N/A

 Combustion chamber 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 Excess air (%) N/A Residence time (sec) at temperature (°F) N/A

 Percent heat recovery N/A Vendor guarantee on incinerator 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 incinerator performance, including parameters monitored

N/A
FORM C-5

AIR POLLUTION CONTROL Not applicable to this facility.V. Thermal Incinerator For each Thermal Incinerator: Thermal Incinerator 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

 Plans to replace or upgrade thermal incinerator N/A
FORM C-6

AIR POLLUTION CONTROLVI. High Velocity Air Filter (HVAF) For each HVAF: HVAF 1 HVAF 2  Process line(s) (identification name/number) 70 70 K5 Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan)

70 Cooling (North Smoke Stripper) (Stack SV-18-11)

70 Cooling (South Smoke Stripper) (Stack SV-18-11)

K5 CoStripp

 Latitude (decimal degrees, six decimal places) 39.1490625 39.1490625 39.14 Longitude (decimal degrees, six decimal places) -94.6151425 -94.6151425 -94.6 Stack or vent height (units) 37.58 ft. 37.58 ft. 42 ft. Stack or vent diameter (units) 1.67 ft. 1.67 ft. 1 ft. Manufacturer and model OC Proprietary Design OC Proprietary Design OC P Date of original installation 1985 1985 Unkn Inlet gas flow rate (acfm @ °F) 5,018 acfm @ 122 °F 5,018 acfm @ 122 °F 6,349 

 Inlet gas temperature (°F) No data available. No data available. No da

 Outlet gas temperature (°F) 100-150 °F 100-150 °F 100-1

 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 No data available. No data available. No da Water spray rate (gpm), if applicable 20 - 60 gpm 20 - 60 gpm 20 - 6 Filter face velocity (acfm/ft2) No data available. No data available. No da

 Maximum pressure drop across mat (in. H2O gauge) No data available. No data available. No da

 Vendor guarantee on HVAF efficiency (attach copy) N/A N/A N/A Method and frequency of filter mad advancement Filters pads are replaced once 

per shift.

Filters pads are replaced once per shift.

Filters per s

 Amount of wastewater generated (gpd) 0 gpd (infrequent discharges) 0 gpd (infrequent discharges) 0 gpd 

 Amount of wastewater recycled (gpd) 100% 100% 100% Amount of wastewater disposed of (gpd) 0 gpd (infrequent discharges) 0 gpd (infrequent discharges) 0 gpd  Method of wastewater disposal N/A N/A N/A
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) 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 (sdig), 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

HVAF 4 HVAF 5 

K5 J6 J6 K5 Cooling (South Smoke Stripper) (Stack SV-08-10)

J6 Cooling (North Smoke Stripper) (Stack SV-10-07)

J6 CoStripp

39.1487397 39.1491186 39.14-94.6140753 -94.6142931 -94.642 ft. 42.50 ft. 42.50 1 ft. 1.67 ft. 1.67 fOC Proprietary Design OC Proprietary Design OC PUnknown Unknown Unkn6,349 acfm @ 139 °F 7,898 acfm @ 121 °F 7,898 No data available. No data available. No da100-150 °F 100-120 °F 100-1No data available. No data available. No daNo data available. No data available. No da<20% <20% <20%No data available. No data available. No da20 - 60 gpm 20 - 60 gpm 20 - 6No data available. No data available. No daNo data available. No data available. No daN/A N/A N/AFilters pads are replaced once per shift.

Filters pads are replaced once per shift.

Filters per s

0 gpd (infrequent discharges) 0 gpd (infrequent discharges) 0 gpd 100% 100% 100%0 gpd (infrequent discharges) 0 gpd (infrequent discharges) 0 gpd N/A N/A N/A
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) 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 (sdig), 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

HVAF 7 HVAF 8 

70 70 7070 Curing (Oven Charge - North HPAF) (Stack SV-18-06)

70 Curing (Oven Charge - South HPAF) (Stack SV-18-

06)

70 CuNorth 

39.1494172 39.1494172 39.14-94.6151708 -94.6151708 -94.642.27 ft. 42.27 ft. 37.84 2.50 ft. 2.50 ft. 2 ft.OC Proprietary Design OC Proprietary Design OC P1986 1984 Unkn9,694 acfm @ 125 °F 9,694 acfm @ 125 °F 9,327 No data available. No data available. No da120-130 °F 120-130 °F 100-1No data available. No data available. No daNo data available. No data available. No da<20% <20% <20%No data available. No data available. No da32.5 - 65.5 gpm 32.5 - 65.5 gpm 32.5 No data available. No data available. No daNo data available. No data available. No daN/A N/A N/AFilters pads are replaced once per shift.

Filters pads are replaced once per shift.

Filters per s

0 gpd (infrequent discharges) 0 gpd (infrequent discharges) 0 gpd 100% 100% 100%0 gpd (infrequent discharges) 0 gpd (infrequent discharges) 0 gpd N/A N/A N/A
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) 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 (sdig), 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

HVAF 10 HVAF 11 

70 K5 K5 70 Curing (Oven Discharge South HPAF) (Stack SV-17-

06)

K5 Curing (Oven Charge North HPAF) (Stack SV-08-15)

K5 CSouth 

15)

39.1491572 39.1490961 39.14-94.6150242 -94.6140361 -94.637.84 ft. 45 ft. 45 ft.2 ft. 2.5 ft. 2.5 ftOC Proprietary Design OC Proprietary Design OC PUnknown 1985 19859,327 acfm @ 132 °F 13,339 acfm @ 147 °F 13,33No data available. No data available. No da100-150 °F 120-130 °F 120-1No data available. No data available. No daNo data available. No data available. No da<20% <20% <20%No data available. No data available. No da32.5 - 65.5 gpm 32.5 - 65.5 gpm 32.5 No data available. No data available. No daNo data available. No data available. No daN/A N/A N/AFilters pads are replaced once per shift.

Filters pads are replaced once per shift.

Filters per s

0 gpd (infrequent discharges) 0 gpd (infrequent discharges) 0 gpd 100% 100% 100%0 gpd (infrequent discharges) 0 gpd (infrequent discharges) 0 gpd N/A N/A N/A
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) 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 (sdig), 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

HVAF 13 HVAF 14 

K5 K5 J6K5 Curing (Oven Discharge North HPAF) (Stack SV-08-11)

K5 Curing (Oven Discharge South HPAF) (Stack SV-08-

11)

J6 CuHPAF

39.1488025 39.1488025 39.14-94.6140422 -94.6140422 -94.640.5 ft. 40.5 ft. 37.75 2.5 ft. 2.5 ft. 1.83 fOC Proprietary Design OC Proprietary Design OC P1987 1987 Unkn6,677 acfm @ 141 °F 6,677 acfm @ 141 °F 10,03No data available. No data available. No da100-150 °F 100-150 °F 120-1No data available. No data available. No daNo data available. No data available. No da<20% <20% <20%No data available. No data available. No da32.5 - 65.5 gpm 32.5 - 65.5 gpm 32.5 No data available. No data available. No daNo data available. No data available. No daN/A N/A N/AFilters pads are replaced once per shift.

Filters pads are replaced once per shift.

Filters per s

0 gpd (infrequent discharges) 0 gpd (infrequent discharges) 0 gpd 100% 100% 100%0 gpd (infrequent discharges) 0 gpd (infrequent discharges) 0 gpd N/A N/A N/A
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) 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 (sdig), 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

HVAF 16 HVAF 17 

J6 J6 J6 J6 Curing (Oven Charge South HPAF) (Stack SV-10-

06)

J6 Curing (Oven Discharge North HPAF) (Stack SV-10-11)

J6 CuSouth 

11)

39.149295 39.14917 39.14-94.6143061 -94.6143386 -94.637.75 ft. 35.58 ft. 35.58 1.83 ft. 1.83 ft. 1.83 fOC Proprietary Design OC Proprietary Design OC PUnknown Unknown Unkn10,033 acfm @ 148 °F 11,165 acfm @ 133 °F 11,16No data available. No data available. No da120-130 °F 100-150 °F 100-1No data available. No data available. No daNo data available. No data available. No da<20% <20% <20%No data available. No data available. No da32.5 - 65.5 gpm 32.5 - 65.5 gpm 32.5 No data available. No data available. No daNo data available. No data available. No daN/A N/A N/AFilters pads are replaced once per shift.

Filters pads are replaced once per shift.

Filters per s

0 gpd (infrequent discharges) 0 gpd (infrequent discharges) 0 gpd 100% 100% 100%0 gpd (infrequent discharges) 0 gpd (infrequent discharges) 0 gpd N/A N/A N/A
FORM C-6

AIR POLLUTION CONTROLVI. High Velocity Air Filter (HVAF) For each HVAF: HVAF 1 HVAF 2  Process line(s) (identification name/number) 70 70 K5 Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan)

70 Cooling (North Smoke Stripper) (Stack SV-18-11)

70 Cooling (South Smoke Stripper) (Stack SV-18-11)

K5 CoStripp

 Quantity of solid waste collected (lbs/yr) 39,000 lbs 39,000 lbs 39,00 Quantity of solid waste recycled (lbs/yr) 0 lbs/yr 0 lbs/yr 0 lbs/ Quantity of solid waste disposed of (lbs/yr) 39,000 lbs 39,000 lbs 39,00 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. 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. Nozzles and flow patterns are checked daily; repairs are completed as needed. Cleaning is performed on a cycle matching machine downtime.

Genefollow that is maintNozzcheckcompCleancycle down

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

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

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

As rereporrepaifailure 

 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) 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 

K5 J6 J6 K5 Cooling (South Smoke Stripper) (Stack SV-08-10)

J6 Cooling (North Smoke Stripper) (Stack SV-10-07)

J6 CoStripp

39,000 lbs 39,000 lbs 39,000 lbs/yr 0 lbs/yr 0 lbs/39,000 lbs 39,000 lbs 39,00Local Solid Waste Landfill Local Solid Waste Landfill Local 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.

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 maintNozzcheckcompCleancycle down

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

None reported in Title V deviation reports. 

None devia

N/A N/A N/ANone 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) 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 7 HVAF 8 

70 70 7070 Curing (Oven Charge - North HPAF) (Stack SV-18-06)

70 Curing (Oven Charge - South HPAF) (Stack SV-18-

06)

70 CuNorth 

39,000 lbs 39,000 lbs 39,000 lbs/yr 0 lbs/yr 0 lbs/39,000 lbs 39,000 lbs 39,00Local Solid Waste Landfill Local Solid Waste Landfill Local 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. Cleaning is performed on a cycle matched to machine downtime.

Genefollow that is maintCleancycle down

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

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

As rereporrepairepairepai

Water Flow Water Flow WateNone 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) 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 10 HVAF 11 

70 K5 K5 70 Curing (Oven Discharge South HPAF) (Stack SV-17-

06)

K5 Curing (Oven Charge North HPAF) (Stack SV-08-15)

K5 CSouth 

15)

39,000 lbs 39,000 lbs 39,000 lbs/yr 0 lbs/yr 0 lbs/39,000 lbs 39,000 lbs 39,00Local Solid Waste Landfill Local Solid Waste Landfill Local 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. Cleaning is performed on a cycle matched to machine downtime.

Genefollow that is maintCleancycle down

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

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

As rereporrepaifailure 

Water Flow Water Flow WateNone 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) 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 13 HVAF 14 

K5 K5 J6K5 Curing (Oven Discharge North HPAF) (Stack SV-08-11)

K5 Curing (Oven Discharge South HPAF) (Stack SV-08-

11)

J6 CuHPAF

39,000 lbs 39,000 lbs 39,000 lbs/yr 0 lbs/yr 0 lbs/39,000 lbs 39,000 lbs 39,00Local Solid Waste Landfill Local Solid Waste Landfill Local 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. Cleaning is performed on a cycle matched to machine downtime.

Genefollow that is maintCleancycle down

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

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

None devia

Water Flow Water Flow WateNone 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) 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 16 HVAF 17 

J6 J6 J6 J6 Curing (Oven Charge South HPAF) (Stack SV-10-

06)

J6 Curing (Oven Discharge North HPAF) (Stack SV-10-11)

J6 CuSouth 

11)

39,000 lbs 39,000 lbs 39,000 lbs/yr 0 lbs/yr 0 lbs/39,000 lbs 39,000 lbs 39,00Local Solid Waste Landfill Local Solid Waste Landfill Local 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. Cleaning is performed on a cycle matched to machine downtime.

Genefollow that is maintCleancycle down

None reported in Title V deviation reports. 

None reported in Title V deviation reports. 

None devia

Water Flow Water Flow WateNone currently approved or 

scheduled at this time.

None currently approved or scheduled at this time.

None sched
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 Stack or vent diameter (units) 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

 Spacing between blades (in.) 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 Vendor guarantee on mist eliminator efficiency (attach copy) N/A Amount of wastewater generated (gpd) N/A
FORM C-7

AIR POLLUTION CONTROLVII. Mist Eliminator Not applicable to this facility. For each Mist Eliminator: Mist Eliminator 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 (various)

 Latitude (decimal degrees, six decimal places) 39.148578 Longitude (decimal degrees, six decimal places) -94.614942 Stack or vent height (units) Roof ht. Stack or vent diameter (units) Various 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) 70 K5  Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan)

70 Forming (70FORMING) K5 Forming (K5FORMINGN 

and K5FORMINGS)

 Latitude (decimal degrees, six decimal places) 39.1493044 (stack 01-07), 

39.1500183 (stack 01-08), 39.1494297 (stack 01-09) and 39.1494853 (stack 01-

10)

39.1492742 (stack 04-11), 39.1493311 (stack 04-12), 39.1494586 (stack 04-14) and 39.1494919 (stack 04-16)

 Longitude (decimal degrees, six decimal places) -94.6147317 (stack 01-07), -

94.6147239 (stack 01-08), -94.6148525 (stack 01-09) and -94.6149111 (stack 01-10)

-94.6138611 (stack 04-11), -94.6141175 (stack 04-12), -94.6141147 (stack 04-14) and -94.6141353 (stack 04-16)

 Stack or vent height (units) 93.40 ft. (stack 01-07), 

100.75 ft. (stack 01-08), 99.40 ft. (stack 01-09) and 93.40 ft. (stack 01-10)

79.18 ft. (stack 04-11), 100.75 ft. (stack 04-12), 92.35 ft. (stack 04-14) and 88.98 ft. (stack 04-16)

 Stack or vent diameter (units) 4.33 ft. (stack 01-07), 4.58 

ft. (stack 01-08), 4.00 ft. (stack 01-09) and 4.33 ft. 

(stack 01-10)

3.42 ft. (stack 04-11), 4.58 ft. (stack 04-12), 3.75 ft. (stack 04-14) and 3.422 ft. (stack 04-16)

Description Drop-Out Boxes with 

Cyclonic Separators

Drop-Out Boxes with Cyclonic Separators
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) Stack or vent diameter (units)

Description

Other APCD 3

7070 Furnace (70FURNACE)39.1496769 (stack 01-03) and 39.1495919 (stack 01-04)-94.6150889 (stack 01-03) and -94.6150906 (stack 01-04)67.11 ft (each)4.00 ft. (each)Batch Wetting
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

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

permit condition was exceeded;

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 Repo

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.

No 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 scope of the existing data provided was the result of consensus reached by EPA, NAIMA and industryrepresentatives. 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.The 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. 
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 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.

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).

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  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 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 Labor ($/yr) for each labor class (hr/hr) for each labor class Utilites (breackdown for each utility) Waste treatment and/or disposal Indirect costs Other (specify)

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

 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.