**FORM A -1** 

**PA RENT COMPA**  **NY INFORMA TION** 

**I. Parent Company / Legal Corporate Owner Information**

1. Legal Parent Company/ Legal Corporate Name Johns Manville 2. Address 717 17th St 3. City Denver 4. State CO 5. Zip Code 80202 6. County Denver

7. Size of Company (approximate number of employ ees including all subsidiaries, branches, and related establishments owned): 6,491 (end of 2009)



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsA-1 10/28/2011**FORM A -2** 

**FA CILITY INFORMA** 

**TION**

**II. Facility Information**

Facility Name Johns Manville W aterville Plant 7 Facility Address Street 7500 Dutch Rd. City Wa terville State OH Zip Code 43566 County Lucas Facility Coordinates Latitude (decimal degrees, six decimal places) 41.525002 Longitude (decimal degrees, six decimal places) -83.720833 Specific location represented (e.g., front door of main building, centroid of property , etc.) Main road entrance to the plant property

Number of employees attached to the wool fiberglass manufacturing facility : See CBI Subm ittal

Design capacity

of the plant (tons/yr) See CBI Subm ittal

Ty pe(s) of process(es) (rotary spin, flame attenuation) at this plant Rotary Spin and Flam e Attenuation

Operation schedule hrs/day 24 days/y r 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) See attachment 1 for Title V Permit

**III. Technical Contact**

Name Carrie Jo Perry Technical Contact Title Complex Environmental Manager Telephone 419-878-1584 Facsimile (Fax) 419-878-1115 Email PerryC@jm.com



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsA-2 10/28/2011**IV. Other**

Is the facility

a major source of HAP? Yes

If No, did the facility take a limit of its potential HAP emissions to avoid classification as a major source: N/A

Does the facility

manufacture other products in addition to wool fiberglass? Yes

If Yes, list the other products manufactured at the facility

. Fiberglass Mat, W ound Sliver Product, High Purity Quartz, Felts & Quartz

Are there any

HAP em issions associated with any co-located facilities? List unit operations, e.g., boiler, and pollutant/emissions. Weinterpret this to seek information on sources of HAPs other than wool fiber glass at the facility rather than co-located facilities. Yes- 9272 Mat Line for formaldehyde.



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsA-2 10/28/2011**FORM B-1**

**PLA NT OPERA** 

**TIONS**

**I. Overview of Plant Operations**

Number 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 Unit 1 Process Unit 2 Process Unit 3 Process Unit 4

Process line identification names or numbers 300X Line 2 (Melters 3&4) 300X Line 1 (Melters 1 & 2) 300X Line 3 (Melter 5) 300X Line 4 (Melter 6)

Ty pe of process line (e.g., rotary spin, flame attenuation) Rotary Spin Rotary Spin Rotary Spin Rotary Spin

Maximum annual production rate (tons/y r) See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal Age of process equipment (y rs) 30 years 30 years 30 years 30 years

Remaining economic life of process line (y rs) Indefinite (due to rebuild capabilities) Indefinite (due to rebuild capabilities) Indefinite (due to rebuild capabilities) Indefinite (due to rebuild capabilities) List of products produced and most recent annual production (tons/y r; specify year) for each product See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

Please attach detailed schematics of each process line. See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-1 Rotary 10/28/2011**FORM B-1**

**PLA NT OPERA** 

**TIONS**

**I. Overview of Plant Operations**

Number of process lines. Include lines that are currently operational or that are temporarily shutdown. (Do not include lines permanently shutdown). 40

For each process line: Process Unit 1 Process Unit 2 Process Unit 3 Process Unit 4

Process line identification names or numbers Microstrand Unit 1 (P035 - P040) Microstrand Unit 2 (P041 - P046) Microstrand Unit 3 (P047 - P052) Microstrand Unit 4 (P053 - P055)

Ty pe of process line (e.g., rotary spin, flame attenuation) Flame Attenuation Flame Attenuation Flame Attenuation Flame Attenuation

Maximum annual production rate (tons/y r) See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

Age of process equipment (y rs) Data Not Available Data Not Available Data Not Available Data Not Available

Remaining economic life of process line (y rs) Indefinite (due to rebuild capabilities) Indefinite (due to rebuild capabilities) Indefinite (due to rebuild capabilities) Indefinite (due to rebuild capabilities)

List of products produced and most recent annual production (tons/y r; specify year) for each product See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

Please attach detailed schematics of each process line. See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-1 P&M Units 1 -10 10/28/2011**FORM B-1**

**PLA NT OPERA** 

**TIONS**

**I. Overview of Plant Operations**

Number of process lines. Include lines that are currently operational or that are temporarily shutdown. (Do not include lines permanently shutdown).

For each process line:

Process line identification names or numbers

Ty pe of process line (e.g., rotary spin, flame attenuation)

Maximum annual production rate (tons/y r)

Age of process equipment (y rs)

Remaining economic life of process line (y rs)

List of products produced and most recent annual production (tons/y r; specify year) for each product

Please attach detailed schematics of each process line. Process Unit 5 Process Unit 6 Process Unit 7 Process Unit 8 Microstrand Unit 5 (P056 - P058) Microstrand Unit 6 (P059 - P061) Microstrand Unit 7

(P062- P064) Microstrand Unit 8

P065 - P067)

Flame Attenuation Flame Attenuation Flame Attenuation Flame Attenuation

See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

Data Not Available Data Not Available Data Not Available Data Not Available

Indefinite (due to rebuild capabilities) Indefinite (due to rebuild capabilities) Indefinite (due to

rebuild capabilities) Indefinite (due to

rebuild capabilities)

See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-1 P&M Units 1 -10 10/28/2011**FORM B-1**

**PLA NT OPERA** 

**TIONS**

**I. Overview of Plant Operations**

Number of process lines. Include lines that are currently operational or that are temporarily shutdown. (Do not include lines permanently shutdown).

For each process line:

Process line identification names or numbers

Ty pe of process line (e.g., rotary spin, flame attenuation)

Maximum annual production rate (tons/y r)

Age of process equipment (y rs)

Remaining economic life of process line (y rs)

List of products produced and most recent annual production (tons/y r; specify year) for each product

Please attach detailed schematics of each process line. Process Unit 9 Process Unit 10 Microstrand Unit 9 (P068 - P070) Microstrand Unit 10

(P071 - P073)

Flame Attenuation Flame Attenuation

See CBI Subm ittal See CBI Subm ittal

Data Not Available Data Not Available

Indefinite (due to rebuild capabilities) Indefinite (due to

rebuild capabilities)

See CBI Subm ittal See CBI Subm ittal

See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-1 P&M Units 1 -10 10/28/2011**FORM B-1**

**PLA NT OPERA** 

**TIONS**

**I. Overview of Plant Operations**

Number of process lines. Include lines that are currently operational or that are temporarily shutdown. (Do not include lines permanently shutdown). 40

For each process line: Process Unit 1 Process Unit 2 Process Unit 3 Process Unit 4

Process line identification names or numbers Microstrand Unit 11 (P074 - P076) Microstrand Unit 12 (P077 - P079) Microstrand Unit 13 (P080 - P082) Microstrand Unit 14 (P083 - P085)

Ty pe of process line (e.g., rotary spin, flame attenuation) Flame Attenuation Flame Attenuation Flame Attenuation Flame Attenuation Maximum annual production rate (tons/y r) See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal Age of process equipment (y rs) Data Not Available Data Not Available Data Not Available Data Not Available

Remaining economic life of process line (y rs) Indefinite (due to rebuild capabilities) Indefinite (due to rebuild capabilities) Indefinite (due to rebuild capabilities) Indefinite (due to rebuild capabilities) List of products produced and most recent annual production (tons/y r; specify year) for each product See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

Please attach detailed schematics of each process line. See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-1 P&M Units 11-20 10/28/2011**FORM B-1**

**PLA NT OPERA** 

**TIONS**

**I. Overview of Plant Operations**

Number of process lines. Include lines that are currently operational or that are temporarily shutdown. (Do not include lines permanently shutdown).

For each process line:

Process line identification names or numbers

Ty pe of process line (e.g., rotary spin, flame attenuation) Maximum annual production rate (tons/y r) Age of process equipment (y rs)

Remaining economic life of process line (y rs) List of products produced and most recent annual production (tons/y r; specify year) for each product

Please attach detailed schematics of each process line. Process Unit 5 Process Unit 6 Process Unit 7 Process Unit 8 Microstrand Unit 15 (P086 - P088) Microstrand Unit 16 (P089 - P091) Microstrand Unit 17

(P092 - P094) Microstrand Unit 18

(P095 - P097)

Flame Attenuation Flame Attenuation Flame Attenuation Flame Attenuation See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal Data Not Available Data Not Available Data Not Available Data Not Available

Indefinite (due to rebuild capabilities) Indefinite (due to rebuild capabilities) Indefinite (due to

rebuild capabilities) Indefinite (due to

rebuild capabilities)

See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-1 P&M Units 11-20 10/28/2011**FORM B-1**

**PLA NT OPERA** 

**TIONS**

**I. Overview of Plant Operations**

Number of process lines. Include lines that are currently operational or that are temporarily shutdown. (Do not include lines permanently shutdown).

For each process line:

Process line identification names or numbers

Ty pe of process line (e.g., rotary spin, flame attenuation) Maximum annual production rate (tons/y r) Age of process equipment (y rs)

Remaining economic life of process line (y rs) List of products produced and most recent annual production (tons/y r; specify year) for each product

Please attach detailed schematics of each process line. Process Unit 9 Process Unit 10 Microstrand Unit 19 (P098 - P100) Microstrand Unit 20

(P101 - P103)

Flame Attenuation Flame Attenuation See CBI Subm ittal See CBI Subm ittal Data Not Available Data Not Available

Indefinite (due to rebuild capabilities) Indefinite (due to

rebuild capabilities)

See CBI Subm ittal See CBI Subm ittal

See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-1 P&M Units 11-20 10/28/2011**FORM B-1**

**PLA NT OPERA** 

**TIONS**

**I. Overview of Plant Operations**

Number of process lines. Include lines that are currently operational or that are temporarily shutdown. (Do not include lines permanently shutdown). 40

For each process line: Process Unit 1 Process Unit 2 Process Unit 3 Process Unit 4

Process line identification names or numbers Microstrand Unit 21 (P104 - P106) Microstrand Unit 22 (P107 - P109) Microstrand Unit 23 (P110 - P111) Microstrand Unit 24 (P112 - P113)

Ty pe of process line (e.g., rotary spin, flame attenuation) Flame Attenuation Flame Attenuation Flame Attenuation Flame Attenuation Maximum annual production rate (tons/y r) See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal Age of process equipment (y rs) Data Not Available Data Not Available Data Not Available Data Not Available

Remaining economic life of process line (y rs) Indefinite (due to rebuild capabilities) Indefinite (due to rebuild capabilities) Indefinite (due to rebuild capabilities) Indefinite (due to rebuild capabilities) List of products produced and most recent annual production (tons/y r; specify year) for each product See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

Please attach detailed schematics of each process line. See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-1 P&M Units 21-30 10/28/2011**FORM B-1**

**PLA NT OPERA** 

**TIONS**

**I. Overview of Plant Operations**

Number of process lines. Include lines that are currently operational or that are temporarily shutdown. (Do not include lines permanently shutdown).

For each process line:

Process line identification names or numbers

Ty pe of process line (e.g., rotary spin, flame attenuation) Maximum annual production rate (tons/y r) Age of process equipment (y rs)

Remaining economic life of process line (y rs) List of products produced and most recent annual production (tons/y r; specify year) for each product

Please attach detailed schematics of each process line. Process Unit 5 Process Unit 6 Process Unit 7 Process Unit 8 Microstrand Unit 25 (P114 - P117) Microstrand Unit 26 (P118 - P120) Microstrand Unit 27

(P121 - P123) Microstrand Unit 28

(P124 - P126)

Flame Attenuation Flame Attenuation Flame Attenuation Flame Attenuation See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal Data Not Available Data Not Available Data Not Available Data Not Available

Indefinite (due to rebuild capabilities) Indefinite (due to rebuild capabilities) Indefinite (due to

rebuild capabilities) Indefinite (due to

rebuild capabilities)

See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-1 P&M Units 21-30 10/28/2011**FORM B-1**

**PLA NT OPERA** 

**TIONS**

**I. Overview of Plant Operations**

Number of process lines. Include lines that are currently operational or that are temporarily shutdown. (Do not include lines permanently shutdown).

For each process line:

Process line identification names or numbers

Ty pe of process line (e.g., rotary spin, flame attenuation) Maximum annual production rate (tons/y r) Age of process equipment (y rs)

Remaining economic life of process line (y rs) List of products produced and most recent annual production (tons/y r; specify year) for each product

Please attach detailed schematics of each process line. Process Unit 9 Process Unit 10 Microstrand Unit 29 (P127 - P132) Microstrand Unit 30

(P133 - P138)

Flame Attenuation Flame Attenuation See CBI Subm ittal See CBI Subm ittal Data Not Available Data Not Available

Indefinite (due to rebuild capabilities) Indefinite (due to

rebuild capabilities)

See CBI Subm ittal See CBI Subm ittal

See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-1 P&M Units 21-30 10/28/2011**FORM B-1**

**PLA NT OPERA** 

**TIONS**

**I. Overview of Plant Operations**

Number of process lines. Include lines that are currently operational or that are temporarily shutdown. (Do not include lines permanently shutdown). 40

For each process line: Process Unit 1 Process Unit 2 Process Unit 3 Process Unit 4

Process line identification names or numbers Microstrand Unit 31 (P139 - P144) Microstrand Unit 32 (P145 - P150) Microstrand Unit 33 (P151 - P156) Microstrand Unit 34 (P157 - P162)

Ty pe of process line (e.g., rotary spin, flame attenuation) Flame Attenuation Flame Attenuation Flame Attenuation Flame Attenuation Maximum annual production rate (tons/y r) See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal Age of process equipment (y rs) Data Not Available Data Not Available Data Not Available Data Not Available

Remaining economic life of process line (y rs) Indefinite (due to rebuild capabilities) Indefinite (due to rebuild capabilities) Indefinite (due to rebuild capabilities) Indefinite (due to rebuild capabilities) List of products produced and most recent annual production (tons/y r; specify year) for each product See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

Please attach detailed schematics of each process line. See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-1 P&M Units 31-40 10/28/2011**FORM B-1**

**PLA NT OPERA** 

**TIONS**

**I. Overview of Plant Operations**

Number of process lines. Include lines that are currently operational or that are temporarily shutdown. (Do not include lines permanently shutdown).

For each process line:

Process line identification names or numbers

Ty pe of process line (e.g., rotary spin, flame attenuation) Maximum annual production rate (tons/y r) Age of process equipment (y rs)

Remaining economic life of process line (y rs) List of products produced and most recent annual production (tons/y r; specify year) for each product

Please attach detailed schematics of each process line. Process Unit 5 Process Unit 6 Process Unit 7 Process Unit 8 Microstrand Unit 35 (P163 - P169) Microstrand Unit 36 (P170 - P176) Microstrand Unit 37

(P177 - P183) Microstrand Unit 38

(P184 - P190)

Flame Attenuation Flame Attenuation Flame Attenuation Flame Attenuation See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal Data Not Available Data Not Available Data Not Available Data Not Available

Indefinite (due to rebuild capabilities) Indefinite (due to rebuild capabilities) Indefinite (due to

rebuild capabilities) Indefinite (due to

rebuild capabilities)

See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-1 P&M Units 31-40 10/28/2011**FORM B-1**

**PLA NT OPERA** 

**TIONS**

**I. Overview of Plant Operations**

Number of process lines. Include lines that are currently operational or that are temporarily shutdown. (Do not include lines permanently shutdown).

For each process line:

Process line identification names or numbers

Ty pe of process line (e.g., rotary spin, flame attenuation) Maximum annual production rate (tons/y r) Age of process equipment (y rs)

Remaining economic life of process line (y rs) List of products produced and most recent annual production (tons/y r; specify year) for each product

Please attach detailed schematics of each process line. Process Unit 9 Process Unit 10 Microstrand Unit 39 (P191 - P197) Microstrand Unit 40

(P198 - P204)

Flame Attenuation Flame Attenuation See CBI Subm ittal See CBI Subm ittal Data Not Available Data Not Available

Indefinite (due to rebuild capabilities) Indefinite (due to

rebuild capabilities)

See CBI Subm ittal See CBI Subm ittal

See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-1 P&M Units 31-40 10/28/2011**FORM B-1**

**PLA NT OPERA** 

**TIONS**

**I. Overview of Plant Operations**

Number of process lines. Include lines that are currently operational or that are temporarilyshutdown. (Do not include lines permanentlyshutdown). 1

For each process line: Process Unit 1 Process line identification names or numbers 2-Meter Melter

Ty pe of process line (e.g., rotaryspin, flame attenuation) Melter for making glass marbles Maximum annual production rate (tons/y r) See CBI Submittal Age of process equipment (y rs) Data not available

Remaining economic life of process line (y rs) Indefinite (due to rebuild capabilities) List of products produced and most recent annual production (tons/y r; specify year) for each product See CBI Submittal

Please attach detailed schematics of each process line. See CBI Submittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-1 2-Meter Melter 10/28/2011**FORM B-2**

**PLA NT OPERA** 

**TIONS**

**II. Process - Raw materials Handling and Storage**

Molten glass preparation Raw materials and proportions bywt (%) Glass Marbles - 100% Method(s) of convey ing each raw material to furnace/pots Marble Hoppers/Bucket Lifts Binder and Additives List each raw material, including premixed materials, in the binder formulation and its proportion bywt (%) N/A List steps in preparing binder, including storage temperature ( °F) and holding time (hrs) N/A Total yearly

consumption of binder (gal/y r) N/A Cost of binder ($/gal) for most recent y ear (specify year) N/A

Are binder storage and mixing tanks vented to outside/inside? N/A 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 N/A



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-2 P&M and Rotary 10/28/2011**FORM B-2**

**PLA NT OPERA** 

**TIONS**

**II. Process - Raw materials Handling and Storage** 2-Meter Melter 300X Lines Molten glass preparation Raw materials and proportions bywt (%) See CBI Submittal Glass Marbles - 100% Method(s) of convey ing each raw material to furnace/pots pneumatic Marble Hoppers/Bucket Lifts Binder and Additives List each raw material, including premixed materials, in the binder formulation and its proportion bywt (%) N/A N/A List steps in preparing binder, including storage temperature ( °F) and holding time (hrs) N/A N/A Total yearly

consumption of binder (gal/y r) N/A N/A Cost of binder ($/gal) for most recent y ear (specify year) N/A N/A

Are binder storage and mixing tanks vented to outside/inside? N/A N/A Method of treating vent air from storage and mix tanks N/A N/A Emission control during liquid raw material transfer from vehicles to storage tanks. N/A N/A Describe future source reduction plans and schedules to reformulate binders; List each constituent, proportions wt (%), cost ($/gal) for reformulation N/A N/A



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-2 Melters 10/28/2011**FORM B-3**

**PLA NT OPERA** 

**TIONS**

**III. Process - Glass Melting Furnace**

For each Glass Melting Furnace: Furnace 1 Furnace 2 Furnace 3 Furnace 4 Process unit identification name/number Microstrand Unit 1 Microstrand Unit 2 Microstrand Unit 3 Microstrand Unit 4 Process line(s) served (identification name/number) P035 - P040 P041 - P046 P047 - P052 P053 - P055 Latitude (decimal degrees, six decimal places) 41.524162 41.524162 41.524162 41.524162 Longitude (decimal degrees, six decimal places) -83.720444 -83.720444 -83.720444 -83.720444 Stack or vent height (units) 40 ft 40 ft 40 ft 40 ft Stack or vent diameter (units) 1.85 ft 1.85 ft 1.85 ft 1.85 ft Manufacturer and model JM Proprietary JM Proprietary JM Proprietary JM Proprietary Date of original installation Data Not Available Data Not Available Data Not Available Data Not Available

Estimate of remaining lifetime (y rs) Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance) Major rebuilds: W hat constitues a major rebuild No major rebuilds No major rebuilds No major rebuilds No major rebuilds Frequency

of a major rebuild N/A N/A N/A N/A Cost of typical major rebuild N/A N/A N/A N/A Date of last major rebuild N/A N/A N/A N/A Purpose of last major rebuild N/A N/A N/A N/A Increase or decrease in emissions N/A N/A N/A N/A Fuel ty pe: electric, gas, or oil Gas Gas Gas Gas Fuel consumption rate (KW /ton of glass or Btu/ton of glass) Data Not Available Data Not Available Data Not Available Data Not Available List HAPs that are in refractory material No refractory No refractory No refractory No refractory Design production rate (tons/day) See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal Actual glass pull rate (tons/day) See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

Vent gas flow rate (acfm @ °F) Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection Temperature (°F) of molten glass in furnace and forehearth (if applicable) See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal Nature and frequency of routine/preventive maintenance procedures See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal Describe process modification(s) since 1999 that reduce

em issions None None None None



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 P&M Units 1-10 10/28/2011Describe future source reduction plans and schedules See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 P&M Units 1-10 10/28/2011**FORM B-3**

**PLA NT OPERA** 

**TIONS**

**III. 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 (y rs) Major rebuilds: W hat 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 ty pe: 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 Describe process modification(s) since 1999 that reduce

em issions Furnace 5 Furnace 6 Furnace 7 Furnace 8 Microstrand Unit 5 Microstrand Unit 6 Microstrand Unit 7 Microstrand Unit 8 P056 - P058 P059 - P061 P062 - P064 P065 - P067

41.524162 41.524162 41.524162 41.524162 -83.720444 -83.720444 -83.720444 -83.720444 40 ft 40 ft 40 ft 40 ft 1.85 ft 1.85 ft 1.85 ft 1.85 ft JM Proprietary JM Proprietary JM Proprietary JM Proprietary Data Not Available Data Not Available Data Not Available Data Not Available Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance)

No major rebuilds No major rebuilds No major rebuilds No major rebuilds N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A Gas Gas Gas Gas

Data Not Available Data Not Available Data Not Available Data Not Available No refractory No refractory No refractory No refractory See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection

See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

None None None None



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 P&M Units 1-10 10/28/2011Describe future source reduction plans and schedules See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 P&M Units 1-10 10/28/2011**FORM B-3**

**PLA NT OPERA** 

**TIONS**

**III. 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 (y rs) Major rebuilds: W hat 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 ty pe: 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 Describe process modification(s) since 1999 that reduce

em issions Furnace 9 Furnace 10 Microstrand Unit 9 Microstrand Unit 10 P068 - P070 P071 - P073

41.524162 41.524162 -83.720444 -83.720444 40 ft 40 ft 1.85 ft 1.85 ft JM Proprietary JM Proprietary Data Not Available Data Not Available Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance)

No major rebuilds No major rebuilds N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A Gas Gas

Data Not Available Data Not Available No refractory No refractory See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection

See CBI Subm ittal See CBI Subm ittal

See CBI Subm ittal See CBI Subm ittal

None None



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 P&M Units 1-10 10/28/2011Describe future source reduction plans and schedules See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 P&M Units 1-10 10/28/2011**FORM B-3**

**PLA NT OPERA** 

**TIONS**

**III. Process - Glass Melting Furnace**

For each Glass Melting Furnace: Furnace 1 Furnace 2 Furnace 3 Furnace 4 Process unit identification name/number Microstrand Unit 11 Microstrand Unit 12 Microstrand Unit 13 Microstrand Unit 14 Process line(s) served (identification name/number) P074 - P076 P077 - P079 P080 - P082 P083 - P085 Latitude (decimal degrees, six decimal places) 41.524162 41.524162 41.524162 41.524162 Longitude (decimal degrees, six decimal places) -83.720444 -83.720444 -83.720444 -83.720444 Stack or vent height (units) 40 ft 40 ft 40 ft 40 ft Stack or vent diameter (units) 1.85 ft 1.85 ft 1.85 ft 1.85 ft Manufacturer and model Data Not Available Data Not Available Data Not Available Data Not Available Date of original installation Data Not Available Data Not Available Data Not Available Data Not Available

Estimate of remaining lifetime (y rs) Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance) Major rebuilds: W hat constitues a major rebuild No major rebuilds No major rebuilds No major rebuilds No major rebuilds Frequency

of a major rebuild N/A N/A N/A N/A Cost of typical major rebuild N/A N/A N/A N/A Date of last major rebuild N/A N/A N/A N/A Purpose of last major rebuild N/A N/A N/A N/A Increase or decrease in emissions N/A N/A N/A N/A Fuel ty pe: electric, gas, or oil Gas Gas Gas Gas Fuel consumption rate (KW /ton of glass or Btu/ton of glass) Data Not Available Data Not Available Data Not Available Data Not Available List HAPs that are in refractory material No refractory No refractory No refractory No refractory Design production rate (tons/day) See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal Actual glass pull rate (tons/day) See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

Vent gas flow rate (acfm @ °F) Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection Temperature (°F) of molten glass in furnace and forehearth (if applicable) See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal Nature and frequency of routine/preventive maintenance procedures See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal Describe process modification(s) since 1999 that reduce

em issions None None None None



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 P&M Units 11-20 10/28/2011Describe future source reduction plans and schedules See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 P&M Units 11-20 10/28/2011**FORM B-3**

**PLA NT OPERA** 

**TIONS**

**III. 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 (y rs) Major rebuilds: W hat 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 ty pe: 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 Describe process modification(s) since 1999 that reduce

em issions Furnace 5 Furnace 6 Furnace 7 Furnace 8 Microstrand Unit 15 Microstrand Unit 16 Microstrand Unit 17 Microstrand Unit 18 P086 - P088 P089 - P091 P092 - P094 P095 - P097

41.524162 41.524162 41.524162 41.524162 -83.720444 -83.720444 -83.720444 -83.720444 40 ft 40 ft 40 ft 40 ft 1.85 ft 1.85 ft 1.85 ft 1.85 ft Data Not Available Data Not Available Data Not Available Data Not Available Data Not Available Data Not Available Data Not Available Data Not Available Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance)

No major rebuilds No major rebuilds No major rebuilds No major rebuilds N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A Gas Gas Gas Gas

Data Not Available Data Not Available Data Not Available Data Not Available No refractory No refractory No refractory No refractory See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection

See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

None None None None



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 P&M Units 11-20 10/28/2011Describe future source reduction plans and schedules See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 P&M Units 11-20 10/28/2011**FORM B-3**

**PLA NT OPERA** 

**TIONS**

**III. 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 (y rs) Major rebuilds: W hat 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 ty pe: 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 Describe process modification(s) since 1999 that reduce

em issions Furnace 9 Furnace 10 Microstrand Unit 19 Microstrand Unit 20 P098 - P100 P101 - P103

41.524162 41.524162 -83.720444 -83.720444 40 ft 40 ft 1.85 ft 1.85 ft Data Not Available Data Not Available Data Not Available Data Not Available Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance)

No major rebuilds No major rebuilds N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A Gas Gas

Data Not Available Data Not Available No refractory No refractory See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection

See CBI Subm ittal See CBI Subm ittal

See CBI Subm ittal See CBI Subm ittal

None None



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 P&M Units 11-20 10/28/2011Describe future source reduction plans and schedules See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 P&M Units 11-20 10/28/2011**FORM B-3**

**PLA NT OPERA** 

**TIONS**

**III. Process - Glass Melting Furnace**

For each Glass Melting Furnace: Furnace 1 Furnace 2 Furnace 3 Furnace 4 Process unit identification name/number Microstrand Unit 21 Microstrand Unit 22 Microstrand Unit 23 Microstrand Unit 24 Process line(s) served (identification name/number) P104 - P106 P107 - P109 P110 - P111 P121 - P113 Latitude (decimal degrees, six decimal places) 41.524162 41.524162 41.524162 41.524162 Longitude (decimal degrees, six decimal places) -83.720444 -83.720444 -83.720444 -83.720444 Stack or vent height (units) 40 ft 40 ft 40 ft 40 ft Stack or vent diameter (units) 1.85 ft 1.85 ft 1.85 ft 1.85 ft Manufacturer and model Data Not Available Data Not Available Data Not Available Data Not Available Date of original installation Data Not Available Data Not Available Data Not Available Data Not Available

Estimate of remaining lifetime (y rs) Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance) Major rebuilds: W hat constitues a major rebuild No major rebuilds No major rebuilds No major rebuilds No major rebuilds Frequency

of a major rebuild N/A N/A N/A N/A Cost of typical major rebuild N/A N/A N/A N/A Date of last major rebuild N/A N/A N/A N/A Purpose of last major rebuild N/A N/A N/A N/A Increase or decrease in emissions N/A N/A N/A N/A Fuel ty pe: electric, gas, or oil Gas Gas Gas Gas Fuel consumption rate (KW /ton of glass or Btu/ton of glass) Data Not Available Data Not Available Data Not Available Data Not Available List HAPs that are in refractory material No refractory No refractory No refractory No refractory Design production rate (tons/day) See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal Actual glass pull rate (tons/day) See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

Vent gas flow rate (acfm @ °F) Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection Temperature (°F) of molten glass in furnace and forehearth (if applicable) See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal Nature and frequency of routine/preventive maintenance procedures See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal Describe process modification(s) since 1999 that reduce

em issions None None None None



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 P&M 21-30 10/28/2011Describe future source reduction plans and schedules See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 P&M 21-30 10/28/2011**FORM B-3**

**PLA NT OPERA** 

**TIONS**

**III. 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 (y rs) Major rebuilds: W hat 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 ty pe: 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 Describe process modification(s) since 1999 that reduce

em issions Furnace 5 Furnace 6 Furnace 7 Furnace 8 Microstrand Unit 25 Microstrand Unit 26 Microstrand Unit 27 Microstrand Unit 28 P114 - P117 P118 - P120 P121 - P123 P124 - P126

41.524162 41.524162 41.524162 41.524162 -83.720444 -83.720444 -83.720444 -83.720444 40 ft 40 ft 40 ft 40 ft 1.85 ft 1.85 ft 1.85 ft 1.85 ft Data Not Available Data Not Available Data Not Available Data Not Available Data Not Available Data Not Available Data Not Available Data Not Available Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance)

No major rebuilds No major rebuilds No major rebuilds No major rebuilds N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A Gas Gas Gas Gas

Data Not Available Data Not Available Data Not Available Data Not Available No refractory No refractory No refractory No refractory See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection

See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

None None None None



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 P&M 21-30 10/28/2011Describe future source reduction plans and schedules See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 P&M 21-30 10/28/2011**FORM B-3**

**PLA NT OPERA** 

**TIONS**

**III. 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 (y rs) Major rebuilds: W hat 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 ty pe: 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 Describe process modification(s) since 1999 that reduce

em issions Furnace 9 Furnace 10 Microstrand Unit 29 Microstrand Unit 30 P127 - P132 P133 - P138

41.52354 41.52354 -83.720131 -83.720131 80 80 7 7 Data Not Available Data Not Available Data Not Available Data Not Available Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance)

No major rebuilds No major rebuilds N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A Gas Gas

Data Not Available Data Not Available No refractory No refractory See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection

See CBI Subm ittal See CBI Subm ittal

See CBI Subm ittal See CBI Subm ittal

None None



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 P&M 21-30 10/28/2011Describe future source reduction plans and schedules See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 P&M 21-30 10/28/2011**FORM B-3**

**PLA NT OPERA** 

**TIONS**

**III. Process - Glass Melting Furnace**

For each Glass Melting Furnace: Furnace 1 Furnace 2 Furnace 3 Furnace 4 Process unit identification name/number Microstrand Unit 31 Microstrand Unit 32 Microstrand Unit 33 Microstrand Unit 34 Process line(s) served (identification name/number) P139 - P144 P145 - P150 P151 - P156 P157 - P162 Latitude (decimal degrees, six decimal places) 41.52354 41.52354 41.52354 41.52354 Longitude (decimal degrees, six decimal places) -83.720009 -83.720009 -83.719902 -83.719902 Stack or vent height (units) 80 80 80 80 Stack or vent diameter (units) 7 7 7 7 Manufacturer and model Data Not Available Data Not Available Data Not Available Data Not Available Date of original installation Data Not Available Data Not Available Data Not Available Data Not Available

Estimate of remaining lifetime (y rs) Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance) Major rebuilds: W hat constitues a major rebuild No major rebuilds No major rebuilds No major rebuilds No major rebuilds Frequency

of a major rebuild N/A N/A N/A N/A Cost of typical major rebuild N/A N/A N/A N/A Date of last major rebuild N/A N/A N/A N/A Purpose of last major rebuild N/A N/A N/A N/A Increase or decrease in emissions N/A N/A N/A N/A Fuel ty pe: electric, gas, or oil Gas Gas Gas Gas Fuel consumption rate (KW /ton of glass or Btu/ton of glass) Data Not Available Data Not Available Data Not Available Data Not Available List HAPs that are in refractory material No refractory No refractory No refractory No refractory Design production rate (tons/day) See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal Actual glass pull rate (tons/day) See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

Vent gas flow rate (acfm @ °F) Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection Temperature (°F) of molten glass in furnace and forehearth (if applicable) See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal Nature and frequency of routine/preventive maintenance procedures See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal Describe process modification(s) since 1999 that reduce

em issions None None None None



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 P&M 31-40 10/28/2011Describe future source reduction plans and schedules See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 P&M 31-40 10/28/2011**FORM B-3**

**PLA NT OPERA** 

**TIONS**

**III. 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 (y rs) Major rebuilds: W hat 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 ty pe: 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 Describe process modification(s) since 1999 that reduce

em issions Furnace 5 Furnace 6 Furnace 7 Furnace 8 Microstrand Unit 35 Microstrand Unit 36 Microstrand Unit 37 Microstrand Unit 38 P163 - P169 P170 - P176 P177 - P183 P184 - P190

41.524101 41.524101 41.524075 41.524075 -83.719009 -83.719009 -83.71888 -83.71888 80 80 80 80 5.5 5.5 5.5 5.5 Data Not Available Data Not Available Data Not Available Data Not Available Data Not Available Data Not Available Data Not Available Data Not Available Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance)

No major rebuilds No major rebuilds No major rebuilds No major rebuilds N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A Gas Gas Gas Gas

Data Not Available Data Not Available Data Not Available Data Not Available No refractory No refractory No refractory No refractory See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection

See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

None None None None



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 P&M 31-40 10/28/2011Describe future source reduction plans and schedules See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 P&M 31-40 10/28/2011**FORM B-3**

**PLA NT OPERA** 

**TIONS**

**III. 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 (y rs) Major rebuilds: W hat 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 ty pe: 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 Describe process modification(s) since 1999 that reduce

em issions Furnace 9 Furnace 10 Microstrand Unit 39 Microstrand Unit 40 P191 - P197 P198 - P204

41.524075 41.524075 -83.718796 -83.718796 80 80 5.5 5.5 Data Not Available Data Not Available Data Not Available Data Not Available Indefinite (due to continued

ma intenance) Indefinite (due to continued

ma intenance)

No major rebuilds No major rebuilds N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A Gas Gas

Data Not Available Data Not Available No refractory No refractory See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

Melting process airflow is drawn into forming and collection Melting process airflow is drawn into forming and collection

See CBI Subm ittal See CBI Subm ittal

See CBI Subm ittal See CBI Subm ittal

None None



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 P&M 31-40 10/28/2011Describe future source reduction plans and schedules See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 P&M 31-40 10/28/2011**FORM B-3**

**PLANT OPERATIONS**

**III. Process - Glass Melting Furnace**

For each Glass Melting Furnace: Furnace 1 Furnace 2 Furnace 3 Furnace 4 Furnace 5

Process unit identification name/number 2- Meter Melter 300X Line 2 (Melters 3&4) 300X Line 1 (Melters 1 & 2) 300X Line 3 (Melter 5) 300X Line 4 (Melter 6)

Process line(s) served (identification name/number) P021 P018 P019 P239 P240 Latitude (decimal degrees, six decimal places) 41.52491 41.524059 41.524059 41.524059 41.524059 Longitude (decimal degrees, six decimal places) -83.720787 -83.72097 -83.72097 -83.72097 -83.72097 Stack or vent height (units) 7.6m 62 ft 62 ft 62 ft 62 ft Stack or vent diameter (units) 0.15m 5 ft 5 ft 5 ft 5 ft Manufacturer and model JM Proprietary JM Proprietary JM Proprietary JM Proprietary JM Proprietary Date of original installation Data not available Data not available Data not available Data not available Data not available

Estimate of remaining lifetime (yrs) Indefinite (due to continued maintenance) Indefinite (due to continued maintenance) Indefinite (due to continued maintenance) Indefinite (due to continued maintenance) Indefinite (due to continued maintenance) Major rebuilds:

W hat constitues a major rebuild JM is not familiar with the term "major rebuild." JM conducts periodic routine maintenace. JM is not familiar with the term "major rebuild." JM conducts periodic routine maintenace. JM is not familiar with the term "major rebuild." JM conducts periodic routine maintenace. JM is not familiar with the term "major rebuild." JM conducts periodic routine maintenace. JM is not familiar with the term "major rebuild." JM conducts periodic routine maintenace. Frequency of a major rebuild N/A N/A N/A N/A N/A Cost of typical major rebuild N/A N/A N/A N/A N/A Date of last major rebuild N/A N/A N/A N/A N/A Purpose of last major rebuild N/A N/A N/A N/A N/A Increase or decrease in emissions N/A N/A N/A N/A N/A Fuel type: electric, gas, or oil Electric Gas/ Electric Gas/ Electric Gas/ Electric Gas/ Electric Fuel consumption rate (KW /ton of glass or Btu/ton of glass) See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal

List HAPs that are in refractory material None Chromium Compounds Chromium Compounds Chromium Compounds Chromium Compounds Design production rate (tons/day) See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal Actual glass pull rate (tons/day) See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal Vent gas flow rate (acfm @ °F) See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal Temperature (°F) of molten glass in furnace and forehearth (if applicable) See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal Nature and frequency of routine/preventive maintenance procedures See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal Describe process modification(s) since 1999 that reduce emissions None None None None None

Describe future source reduction plans and schedules See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal

EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 Melters 10/28/2011**FORM B-4**

**PLA NT OPERA** 

**TIONS**

**IV. Process - Forming -- Rotary Spin / Flame A ttenuation** 

For each Forming Operation -- Rotary Spin/Flame Attenuation Forming Operation 1 Forming Operation 2 Forming Operation 3

Process unit identification name/number 300X Line 2 (Melters 3&4) 300X Line 1 (Melters 1 & 2) 300X Line 3 (Melter 5) Process line(s) served (identification name/number) P018 P019 P239 Latitude (decimal degrees, six decimal places) 41.524059 41.524059 41.524059 Longitude (decimal degrees, six decimal places) -83.72097 -83.72097 -83.72097 Stack or vent height (units) 62 ft 62 ft 62 ft Stack or vent diameter (units) 5 ft 5 ft 5 ft Number of fiber forming devices (spinners) per line. See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal Method of attenuating fiber (e.g., air, flame, or air and flame). Indicate ty pe of burner used (if flame). See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal Is there a forehearth between the furnace and the forming section? No No No Major rebuilds:

W hat constitues a major rebuild JM is not familiar with the term "major rebuild." JM conducts periodic routine

ma intenace. JM is not familiar with the term "major rebuild." JM conducts periodic routine

ma intenace. JM is not familiar with the term "major rebuild." JM conducts periodic routine

ma intenace. Frequency

of a major rebuild N/A N/A N/A Cost of typical major rebuild N/A N/A N/A Date of last major rebuild N/A N/A N/A Purpose of last major rebuild N/A N/A N/A Increase or decrease in emissions N/A N/A N/A If modular, number of modules and plenums 2 2 1 Presence of water overspray and application rate (gpm) N/A N/A N/A Binder applied and application rate (gpm) N/A N/A N/A Other material applied and application rate (gpm) N/A N/A N/A Temperature of glass fiber when binder is applied (°F) N/A N/A N/A Temperature of binder when applied to fibers (°F) N/A N/A N/A Method of evenly

distributing fibers onto forming converyor Airflow Airflow Airflow Formed mat thickness (in.) See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal

Forming air flow rate (acfm @ °F) Approx. 32,000 acfm at 85 °F per APC unit Approx. 32,000 acfm at 85 °F per APC unit Approx. 32,000 acfm at 85 °F per APC unit



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-4 10/28/2011Percent of forming air recirculated and percent exhausted 100% exhausted 100% exhausted 100% exhausted

Nature and frequency of routine/preventive maintenance procedures See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal Describe process modification(s) since 1999 that reduce

em issions None None None Describe future source reduction plans and schedules See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-4 10/28/2011**FORM B-4**

**PLA NT OPERA** 

**TIONS**

**IV. Process - Forming -- Rotary Spin / Flame A ttenuation** 

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 ty pe of burner used (if flame). Is there a forehearth between the furnace and the forming section? Major rebuilds:

W hat 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 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 converyor Formed mat thickness (in.)

Forming air flow rate (acfm @ °F) Forming Operation 4

300X Line 4 (Melter 6) P240 41.524059

-83.72097 62 ft 5 ft See CBI Subm ittal

See CBI Subm ittal

No

JM is not familiar with the term "major rebuild." JM conducts periodic routine

ma intenace. N/A N/A N/A N/A N/A 1 N/A N/A N/A N/A N/A Airflow See CBI Subm ittal Approx. 32,000 acfm at 85 °F per APC unit



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-4 10/28/2011Percent of forming air recirculated and percent exhausted

Nature and frequency of routine/preventive maintenance procedures Describe process modification(s) since 1999 that reduce

em issions Describe future source reduction plans and schedules 100% exhausted

See CBI Subm ittal

None See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-4 10/28/2011**FORM B-5**

**PLA NT OPERA** 

**TIONS**

**V. Process - Curing**

For each Curing Oven: Curing Oven 1 Curing Oven 2 Curing Oven 3 Process unit identification name/number N/A N/A N/A

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: W hat 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 ty pe: electric, gas, or oil Fuel consumption rate (KW /hr or BTU/hr) 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

ma intenance procedures Describe process modification(s) since 1999 that reduce emissions Describe future source reduction plans and schedules



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-5 10/28/2011**FORM B-6**

**PLA NT OPERA** 

**TIONS**

**VI. Process - Cooling**

For each Cooling Operation: Cooling Operation 1 Cooling Operation 2 Cooling Operation 3 Process unit identification name/number N/A N/A N/A

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) Nature and frequency of routine/preventive

ma intenance procedures Describe process modification(s) since 1999 that reduce emissions

Describe future source reduction plans and schedules



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-6 10/28/2011**FORM B-7**

**PLA NT OPERA** 

**TIONS**

**VII. Process - Use of Solvents**

Use of Solvents

Volatile solvents used at your facility (where and how used) By agreement this question was limited to HAP containing solvents. W e interpret this question to applyto wool fiberglass lines, from melting through cooling. None List each solvent used and quantity(gal/y r) N/A Emission control device(s) used to control emissions from solvent usage/storage? N/A



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-7 10/28/2011**FORM B-8**

**PROCESS OPERA TIONS** 

VIII. Pollution Prevention

Please describe any

work practices, pollution prevention techniques, and control strategies evaluated and/or implemented at each process unit at your facility

(e.g., binder reformulation, alternative fuels usage, etc.) to reduce emissions of PM and HAPs y ou identified in Form E. You m ust specify

the year in which the facility im plem ented the practice/technique and identifythe emission reductions (if measured) from these practices/techniques. JM objects to this question in that it is unbounded in time. Weinterpret this question, like similar questions in the ICR, to seek data since 1999. W ith that interpretation, JM responds that there have been none.



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-8 10/28/2011**FORM C-1**

**AI R POLLUTION CONTROL** 

**I. Electrostatic Precipitator (ESP)** N/A

For each ESP: ESP 1 ESP 2 ESP 3 Process line(s) (identification name/number) Equipm ent/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan) Latitude (decimal degrees, six decimal places) Longitude (decimal degrees, six decimal places) Stack or vent height (units) Stack or vent diameter (units) Manufacturer and model Date of original installation Number of collection plates and configuration Gas flow rate to ESP (acfm @ °F) Inlet gas temperature ( °F) Outlet gas temperature ( °F) Inlet grain loading (gr/dscf) Outlet grain loading (gr/dscf) Average stack opacity (%) Pressure drop across ESP (in. H 2 O gauge) Plate area (ft2 ) Vendor guarantee on ESP efficency (attach copy) Method of plate cleaning and frequency Flow rate of plate washwater to ESP (gpm), if applicable Temperature of plate washwater to ESP ( °F), if applicable Source of plate washwater used for cleaning, if applicable Concentration (mg/l) of dissolved and suspended solids in plate washwater, if applicable Conditioning agents used and amounts (in gpm or lbs/hr), if applicable Amount of wastewater generated (gpd), if applicable Amount of wastewater recycled (gpd), if applicable Amount of wastewater disposed of (gpd), if applicable Method of wastewater disposal, if applicalbe Quantity

of solid waste collected (lbs/yr) Quantitiy

of solid waste recycled (lbs/y r) Quantity

of solid waste disposed of (lbs/y r)



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsC-1 10/28/2011Method of solid waste disposal

Nature and frequency of routine/preventive maintenance procedures Problems experienced with control device within the last five ye ars; how were problems solved? Continuous monitoring method(s) used to monitor ESP performance, including parameters monitored Describe any

plans to replace or upgrade ESP



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsC-1 10/28/2011**FORM C-2**

**AI R POLLUTION CONTROL** 

**II. Scrubber**

For each Scrubber: Scrubber 1 Scrubber 2 Scrubber 3 Process line(s) (identification name/number) Ducon 1 Ducon 2 Ducon 3

Equipm ent/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan) Microstrand Units 29, 30, 31, 32 or 33 (Backup Control) Microstrand Units 29, 30, 31, 32 or 33 (Backup Control) Microstrand Units 29, 30, 31, 32 or 33 (Backup Control) Latitude (decimal degrees, six decimal places) 41.52404 41.52404 41.524044 Longitude (decimal degrees, six decimal places) -83.72094 -83.721001 -83.72097 Stack or vent height (units) 62 62 62 Stack or vent diameter (units) 5.67 5.67 5.67 Manufacturer and model Ducon Ducon Ducon Date of original installation 6/1/1985 6/1/1985 6/1/1986 Ty pe (e.g., venturi, orifice) Venturi Spray Chamber Spray Chamber Gas flow rate to scrubber (acfm @ °F) 35000acfm @ 85°F 35000acfm @ 85°F 35000acfm @ 85°F Inlet gas temperature (°F) 133 133 275 Outlet gas temperature (°F) 100 115 116 Inlet grain loading (gr/dscf) No data available No data available No data available Outlet grain loading (gr/dscf) No data available 0.0011 0.0024 Average stack opacity (%) 0 0 0 W ater flow rate to scrubber (gpm) 50 50 50 Percent of scrubber water from recycled wastewater 95 - 100% 95 - 100% 95 - 100%

Source of scrubbing water and type of pretreatment. Substance(s) added as part of pretreatment and amount used (gpm or lbs/hr) Softened City W ater Softened City W ater Softened City W ater HAP composition of wastewater (mg/L) None known None known None known Concentration (mg/L) of dissolved and suspended solids in scrubbing water No data available No data available No data available Scrubbing water temperature (°F) Am bient Am bient Am bient Liquid/gas ratio (gal/10 3acfm) ~ 1.43 gal/10 3acfm ~ 1.43 gal/10 3acfm ~ 1.43 gal/10 3acfm Pressure drop across scrubber (in. H 2 O gauge) 2-6 2-6 2-6 Amount of wastewater generated (gpd) No data available No data available No data available Amount of wastewater recycled (gpd) No data available No data available No data available Amount of wastewater disposed of (gpd) No data available No data available No data available Method of wastewater disposal POTW POTW POTW Quantity

of solid waste collected (lbs/yr) No data available No data available No data available Quantity

of solid waste recycled (lbs/y r) 0 0 0



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsC-2 10/28/2011Quantity of solid waste disposed of (lbs/y r) No data available No data available No data available Method of solid waste disposal Filter Press and Landfill Filter Press and Landfill Filter Press and Landfill Vendor guarantee on scrubber efficiency (attach copy) None None None

Nature and frequency of preventive maintenance procedures Scrubber are cleaned out once per year,
ma intenance performed as needed Scrubber are cleaned out once per year,
ma intenance performed as needed Scrubber are cleaned out once per year,
ma intenance performed as needed Problems experienced with control device within the last five years; how were problem s solved? Dried fiber in stacks (routine water washes) Dried fiber in stacks (routine water washes) Dried fiber in stacks (routine water washes)

Continuous monitoring method(s) used to monitor scrubber performance, including parameters monitored Pressure drop across scrubber (monitored but not recorded continuously); Scrubber flowrate (monitored but not recorded continuously) Pressure drop across scrubber (monitored but not recorded continuously); Scrubber flowrate (monitored but not recorded continuously) Pressure drop across scrubber (monitored but not recorded continuously); Scrubber flowrate (monitored but not recorded continuously) Plans to replace or upgrade scrubber See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsC-2 10/28/2011**FORM C-2**

**AI R POLLUTION CONTROL** 

**II. Scrubber**

For each Scrubber: Process line(s) (identification name/number)

Equipm ent/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 Ty pe (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 (%) W ater 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/10 3acfm) Pressure drop across scrubber (in. H 2 O 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/y r) Scrubber 4 Scrubber 5 Scrubber 6 Ducon 4 Ducon 5 CleanGas 6

Rotary Lines 1, 2, 3 and/or 4 Rotary Lines 1, 2, 3 and/or 4 Rotary Lines 1, 2, 3 and/or 4 41.524067 41.524059 41.524059 -83.721077 -83.721001 -83.72097 62 62 62 5.67 5.67 5 Ducon Ducon Clean Gas 6/1/1987 6/1/1985 8/1/1995 Spray Chamber Spray Chamber Spray Chamber 35000acfm @ 85°F 35000acfm @ 85°F 35000acfm @ 85°F 200 133 133 82.5 86 92 No data available No data available No data available 0.0057 0.0044 0.0054 0 0 0 50 50 50 95 - 100% 95 - 100% 95 - 100%

Softened City

W ater Softened City W ater Softened City W ater None known None known None known

No data available No data available No data available Am bient Am bient Am bient ~ 1.43 gal/10 3acfm ~ 1.43 gal/10 3acfm ~ 1.43 gal/10 3acfm 2-6 2-6 2-6
No data available No data available No data available No data available No data available No data available No data available No data available No data available POTW POTW POTW No data available No data available No data available 0 0 0



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsC-2 10/28/2011Quantity of solid waste disposed of (lbs/y r) Method of solid waste disposal Vendor guarantee on scrubber efficiency (attach copy)

Nature and frequency of preventive maintenance procedures Problems experienced with control device within the last five years; how were problem s solved?

Continuous monitoring method(s) used to monitor scrubber performance, including parameters monitored Plans to replace or upgrade scrubber No data available No data available No data available Filter Press and Landfill Filter Press and Landfill Filter Press and Landfill None None None Scrubber are cleaned out once per year,
ma intenance performed as needed Scrubber are cleaned out once per year,
ma intenance performed as needed Scrubber are cleaned out once per year,
ma intenance performed as needed Dried fiber in stacks (routine water washes) Dried fiber in stacks (routine water washes) Dried fiber in stacks (routine water washes)

Pressure drop across scrubber (monitored but not recorded continuously); Scrubber flowrate (monitored but not recorded continuously) Pressure drop across scrubber (monitored but not recorded continuously); Scrubber flowrate (monitored but not recorded continuously) Pressure drop across scrubber (monitored but not recorded continuously); Scrubber flowrate (monitored but not recorded continuously) See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsC-2 10/28/2011**FORM C-3**

**AI R POLLUTION CONTROL** 

**III. Mechanical Collector**

For each Mechanical Collector: Mechanical Collector 1 Process line(s) (identification name/number) EMC Equipm ent/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan) Microstrand Units 1 -28 (P035 - P126) Latitude (decimal degrees, six decimal places) 41.524162 Longitude (decimal degrees, six decimal places) -83.720444 Stack or vent height (units) 40 ft Stack or vent diameter (units) 1.85 ft Manufacturer and model JM Proprietary Date of original installation 1958

Ty pe of mechanical collector Wi re drums with water spray cleaning Gas flow rate to collector (acfm @ °F) No Data Available Inlet gas temperature (°F) No Data Available Outlet gas temperature (°F) 140°F Inlet grain loading (gr/dscf) No Data Available Outlet grain loading (gr/dscf) 0.0054 Average stack opacity (%) 0 Overall pressure drop (in. H 2 O gauge) 1.5 - 3.5 Vendor guarantee on mechanical collector efficiency (attach copy) N/A Quantity

of solid waste collected (lbs/yr) No Data Available Quantity

of solid waste recycled (lbs/y r) 0 Quantity

of solid waste disposed of (lbs/y r) No Data Available Method of solid waste disposal Landfill

Nature and frequency of preventive maintenance procedures EMC are cleaned out once per year, maintenance performed as needed Problems experienced with control device within the last five ye ars; how were problems solved? Dried fiber in stacks (routine water washes)

Continuous monitoring method(s) used to monitor performance, including parameters monitored Pressure drop across system (monitored but not recorded continuously)



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsC-3 10/28/2011Plans to replace or upgrade mechanical collector See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsC-3 10/28/2011**FORM C-4**

**AI R POLLUTION CONTROL** 

**IV. Fabric Filter**

For each Fabric Filter: Fabric Filter 1 Fabric Filter 2 Fabric Filter 3 Process line(s) (identification name/number) Osprey 61 Osprey 62 Osprey 63

Equipm ent/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan) Microstrand Units 29 & 30 Microstrand Units 31 & 32 Microstrand Units 33 & 34 Latitude (decimal degrees, six decimal places) 41.52354 41.52354 41.52354 Longitude (decimal degrees, six decimal places) -83.720131 -83.720009 -83.719902 Stack or vent height (units) 80 80 80 Stack or vent diameter (units) 7 7 7 Manufacturer and model Osprey Osprey Osprey Date of original installation 10/1/1995 10/1/1995 10/1/1995 Number of compartments 2 2 2 Number of bags per compartment 1 1 1 Filter material and coatings applied Carpet Filter Media Carpet Filter Media Carpet Filter Media Fabric weight (oz/yd 2 ) 17 17 17 Filter surface area (ft2 ) 628 628 628 Gas flow rate to filter (acfm @ °F) 45200 45200 45200 Inlet gas temperature (°F) 300 300 300 Outlet gas temperature (°F) 300 295 295 Inlet grain loading (gr/dscf) Data not available Data not available Data not available Outlet grain loading (gr/dscf) 0.0023 0.0023 Data not available Average stack opacity (%) 0 0 0 Overall pressure drop (in. H 2 O gauge) 0.5 - 5 0.5-5 0.5-5

Method and frequency of bag cleaning Fabric filter replacements based on drop in pressure across filter. Fabric filter replacements based on drop in pressure across filter. Fabric filter replacements based on drop in pressure across filter. Vendor guarantee on fabric filter efficiency (attach copy) None None None Quantity

of solid waste collected (lbs/yr) No Data Available No Data Available No Data Available Quantity

of solid waste recycled (lbs/y r) 0 0 0 Quantity

of solid waste disposed of (lbs/y r) No Data Available No Data Available No Data Available Method of solid waste disposal Landfill Landfill Landfill Nature and frequency of preventive maintenance procedures Filter media is replaced every 2-3 months Filter media is replaced every 2-3 months Filter media is replaced every 2-3 months



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsC-4 10/28/2011Problems experienced with control device within the

last five years; how were problems solved? Holes in media; Media repaired or replaced Holes in media; Media repaired or replaced Holes in media; Media repaired or replaced

Continuous monitoring method(s) used to monitor performance, including parameters monitored Pressure drop across media (monitored but not recorded continuously) Pressure drop across media (monitored but not recorded continuously) Pressure drop across media (monitored but not recorded continuously) Plans to replace or upgrade fabric filter See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsC-4 10/28/2011**FORM C-4**

**AI R POLLUTION CONTROL** 

**IV. Fabric Filter**

For each Fabric Filter: Process line(s) (identification name/number)

Equipm ent/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/yd 2 ) 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. H 2 O gauge)

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

of solid waste collected (lbs/yr) Quantity

of solid waste recycled (lbs/y r) Quantity

of solid waste disposed of (lbs/y r) Method of solid waste disposal Nature and frequency of preventive maintenance procedures Fabric Filter 4 Fabric Filter 5 Fabric Filter 6 Osprey 64 Osprey 65 Osprey 66

Microstrand Units 35 & 36 Microstrand Units 37 & 38 Microstrand Units 39 & 40 41.524101 41.524075 41.524075 -83.719009 -83.71888 -83.718796 80 80 80 5.5 5.5 5.5 Osprey Osprey Osprey 1/1/1996 1/1/1996 1/1/1996 2 2 2 1 1 1 Carpet Filter Media Carpet Filter Media Carpet Filter Media 17 17 17 628 628 628 45200 44760 35000 300 325 325 300 300 300 Data not available Data not available Data not available Data not available Data not available Data not available 0 0 0 0.5-5 0.5-5 0.5-5 Fabric filter replacements based on drop in pressure across filter. Fabric filter replacements based on drop in pressure across filter. Fabric filter replacements based on drop in pressure across filter.

None None None No Data Available No Data Available No Data Available 0 0 0 No Data Available No Data Available No Data Available Landfill Landfill Landfill Filter media is replaced every 2-3 months Filter media is replaced every 2-3 months Filter media is replaced every 2-3 months



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsC-4 10/28/2011Problems 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 Holes in media; Media repaired or replaced Holes in media; Media repaired or replaced Holes in media; Media repaired or replaced
Pressure drop across media (monitored but not recorded continuously) Pressure drop across media (monitored but not recorded continuously) Pressure drop across media (monitored but not recorded continuously) See CBI Subm ittal See CBI Subm ittal See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsC-4 10/28/2011**FORM C-4**

**AI R POLLUTION CONTROL** 

**IV. Fabric Filter**

For each Fabric Filter: Process line(s) (identification name/number)

Equipm ent/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/yd 2 ) 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. H 2 O gauge)

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

of solid waste collected (lbs/yr) Quantity

of solid waste recycled (lbs/y r) Quantity

of solid waste disposed of (lbs/y r) Method of solid waste disposal Nature and frequency of preventive maintenance procedures Fabric Filter 7 2-Meter Melter Baghouse

2-Meter Melter 41.52491 -83.720787 7.6m 0.15m Unknown 1/1/1990 1 1 Data Not Available Data Not Available Data Not Available Data Not Available Data Not Available Data Not Available Data Not Available Data Not Available 0 Data Not Available

Replace as needed

None No Data Available 0 No Data Available Landfill Filter media is replaced every 2-3 months



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsC-4 10/28/2011Problems 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 Data Not Available

None See CBI Subm ittal



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsC-4 10/28/2011**FORM C-5**

**AI R POLLUTION CONTROL** 

**V. Thermal Incinerator** N/A

For each Thermal Incinerator: Thermal Incinerator 1 Thermal Incinerator 2 Thermal Incinerator 3 Process line(s) (identification name/number)

Equipm ent/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 Fuel ty pe: gas or oil Fuel consumption rate (BTU/hr) Inlet gas flow rate (acfm @ °F) Inlet gas temperature (°F) Combustion chamber gas temperature (°F) Outlet gas temperature (°F) Inlet grain loading (gr/dscf) Outlet grain loading (gr/dscf) Average stack opacity (%) Excess air (%) Residence time (sec) at temperature (°F) Percent heat recovery Vendor guarantee on incinerator efficiency (attach copy) Nature and frequency of preventive maintenance procedures Problems experienced with control device within the last five years; how were problems solved?

Continuous monitoring method(s) used to monitor incinerator performance, including parameters monitored Plans to replace or upgrade thermal incinerator



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsC-5 10/28/2011**FORM C-6**

**AI R POLLUTION CONTROL** 

**VI. High Velocity A ir Filter (HVA** **F)** N/A

For each HVAF: HVAF 1 HVAF 2 HVAF 3 Process line(s) (identification name/number)

Equipm ent/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 (%) W ater spray

pressure (sdig), if applicable W ater spray

rate (gpm), if applicable Filter face velocity

(acfm/ft2 )

Maximum pressure drop across mat (in. H 2 O gauge)

Vendor guarantee on HVAF efficiency (attach copy) Method and frequency of filter mad advancement Amount of wastewater generated (gpd) Amount of wastewater recycled (gpd) Amount of wastewater disposed of (gpd) Method of wastewater disposal Quantity

of solid waste collected (lbs/yr) Quantity

of solid waste recycled (lbs/y r) Quantity

of solid waste disposed of (lbs/y r) Method of solid waste disposal Nature and frequency of preventive maintenance procedures



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsC-6 10/28/2011Problems 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



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsC-6 10/28/2011**FORM C-7**

**AI R POLLUTION CONTROL** 

**VII. Mist Eliminator** N/A

For each Mist Eliminator: Mist Eliminator 1 Mist Eliminator 2 Mist Eliminator 3 Process line(s) (identification name/number) Equipm ent/process(es) controlled. Include emission point designations (e.g., E3, E4 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 Ty pe of mist eliminator Gas flow rate to mist eliminator (acfm @ °F) Inlet gas temperature (°F) Outlet gas temperature (°F) Inlet grain loading (gr/dscf) Outlet grain loading (gr/dscf) Average stack opacity (%) Velocity

in m ist elim inator (ft/sec) Pressure drop (in. H 2 O gauge) For chevron blade mist eliminators: Spacing between blades (in.) W ashing frequency of blades For mesh pad mist eliminators: Number of pads or elements Thickness of pad (in.) or element dimensions Density

of pad, (lb/ft 3 ) W ashing frequency of pad

Vendor guarantee on mist eliminator efficiency (attach copy) Amount of wastewater generated (gpd) Amount of wastewater recycled (gpd) Amount of wastewater disposed of (gpd) Method of wastewater disposal Quantity

of solid waste collected (lbs/yr) Quantity

of solid waste recycled (lbs/y r)



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsC-7 10/28/2011Quantity of solid waste disposed of (lbs/y r) Method of solid waste disposal

Nature and frequency of preventive maintenance procedures Problems experienced with control device within the last five ye ars; how were problems solved? Continuous monitoring method(s) used to monitor mist eliminator performance, including parameters monitored Plans to replace or upgrade mist eliminator



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsC-7 10/28/2011**FORM C-8**

**AI R POLLUTION CONTROL** 

**VIII. Ventilation System** N/A

For each Ventilation System: Ventilation System 1 Ventilation System 2 Ventilation System 3 Process line(s) (identification name/number) Equipm ent/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan) Latitude (decimal degrees, six decimal places) Longitude (decimal degrees, six decimal places) Stack or vent height (units) Stack or vent diameter (units) For general or building ventilation: Ventilation system used Airflow control system used Number of air changes per hour For unit or local ventilation: Enclosure or hood design used Volume of enclosure or hood Capture velocity (ft/sec) Distance between hood and emission source (ft)



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsC-8 10/28/2011**FORM C-9**

**AI R POLLUTION CONTROL** 

**IX. Other** N/A

For each Other Air Pollution Control Device (APCD): Other APCD 1 Other APCD 2 Other APCD 3 Process line(s) (identification name/number) Equipm ent/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



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsC-9 10/28/2011**FORM D**

**PROCESS LINE STA RTUP A** **ND SHUTDOWN**

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; **No excess emission events during periods of startup and shutdown.** B. A description of the event, including identification of the

em issions source or sources associated with the startup or shutdown; **N/A** C. W hether any

permit condition was exceeded and, if so, what permit condition was exceeded; **N/A**

D. W hether 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; **N/A** E. The duration of the event; **N/A** F. The actions taken to minimize emissions during the event, including the use of any backup control systems; **N/A** 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 ; **N/A** H. W hether 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; **N/A** 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

mo nitoring, collected during each period of SS. **Al l required Title V monitoring data would be collected.**  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.



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsD 10/28/2011If 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

ty pes of startup or shutdown events that you have been able to elim inate? If so, please describe the type of event and explain how these events were elim inated. **N/A** 3. Please submit a copy of your SS plan if you are required to develop one. **No plan required** 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 m onitoring data, including control system parameter monitoring, collected during periods of SS over the last 5 ye ars. **N/A** 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 m inim ize

em issions during the event; and how would compliance be determined and/or monitored. **No**



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsD 10/28/2011**FORM E**

**PRESENCE OF A IR POLLUTA** **NTS IN EMISSION POINTS a** 

Please 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 em issions data. **Me lting Furnace**  **Forming Curing**  **Cooling** 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)
Formaldehyde
Phenol
Methanol Other organic HAP 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 representative existing emissions data provided from fiber glass companies included test results for the following pollutants: formaldehyde, methanol, phenol, particulate

ma tter, hydrogen fluoride, metals (antimony , arsenic, beryllium , cadmium, chromium, cobalt, lead, manganese, nickel, and selenium), mercury , and hexavalent chromium. The representative existing emissions data provided from mineral wool companies included test results for the following pollutants: formaldehyde, methanol, phenol, particulate matter, carbon monoxide, carbony l sulfide, hydrogen fluoride, metals (antimony , arsenic, beryllium , cadmium, chromium, cobalt, lead, manganese, nickel, and selenium ), mercury , and hexavalent chromium. The scope of the existing data provided was the result of consensus reached by EPA, NAIMA, and industry representatives. In addition to the existing data submitted to EPA, extensive new emissions data is being collected from virtually all companies through the “BTEC, Inc. Quality Assurance Project Plan for the Mineral W ool and W ool Fiberglass Emissions Test Program.” This Test Program will collect and subm it to EPA, through EPA’s Electronic Reporting Tool, representative emissions data for the following pollutants: formaldehyde, methanol, phenol, particulate matter, carbon monoxide, carbony l sulfide, hydrogen fluoride,

me tals (antimony , arsenic, beryllium , cadmium, chromium, cobalt, lead, manganese, nickel, and selenium), mercury , and hexavalent chromium.



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsE 10/28/2011**FORM F-1**

**COST**

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

For each Process Unit: Process Unit 1 Process Unit ID All Units Process Line ID

**II. Capital Costs**

Base year JM objects to this request in its entirety

because it seeks information that is not relevant to the EPA Adm inistrator’s review obligations pursuant to Clean Air Act Section 112(d)(6) and 112(f)(2). Total capital cost, including costs for individual pieces, if available. See Above **III. A nnual Operating Costs**  Base year (most recent fiscal year) See Above Total annual operating costs See Above

Maintenance materials and replacement parts (specify costs by item ) See Above Raw m aterials costs See Above Labor ($/yr) for each labor class See Above (hr/hr) for each labor class See Above Utilities (breakdown for each utility) See Above Natural Gas See Above Electric See Above Wa ter See Above W aste treatment and/or disposal See Above Costs associated with any work practices and pollution prevention techniques that are employed at your facility See Above Savings associated with heat recovery and wastewater and/or solid waste returned to process from APCD (or sold to another user) See Above Indirect costs See Above



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsF-1 10/28/2011Other (specify) warewhouse allocation, general plant allocation, and

em ployee benefits See Above

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 provi See Above

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

Can your product(s) be substituted by another product(s)? If so, please list yo ur product(s) and substituted product(s). No

**Footnotes** 1.) Asset has been running prior to 1970 which the financial are not available 2.) Per guidance from Corporate, we selected 2008 as the Base Year because of Footnote 1.) and because of the curtailment in 2009. 2008 is the

mo st current year in which the asset was running full year. 3.) Excluded hrs as we allocate maintenance based on work order data and allocate warehouse labor based on production volume.



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsF-1 10/28/2011**FORM F-2**

**COST**

**I. A ir Pollution Control Device (A** **PCD)** See form F-1

For each APCD: APCD 1 APCD ID Process Unit ID

**II. Capital Costs**

Base year JM objects to this request in its entirety because it seeks information that is not relevant to the EPA Adm inistrator’s review obligations pursuant to Clean Air Act Section 112(d)(6) and 112(f)(2). APCD equipm ent purchase cost and what was included See Above List the cost for each piece of auxiliary equipm ent for each APCD not included above See Above Installation cost See Above Land purchase cost See Above Total capital cost See Above Method of financining APCD See Above Retrofit installation See Above Field erected or modular See Above

**III. A nnual Operating Costs**  Base year (most recent fiscal year) See Above Maintenance materials and replacement parts (specify costs by item ) See Above Raw m aterials costs See Above Labor ($/yr) for each labor class See Above (hr/hr) for each labor class See Above Utilites (breackdown for each utility) See Above W aste treatment and/or disposal See Above Indirect costs See Above



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsF-2 10/28/2011Other (specify) See Above

Total annual operating cost (most recent fiscal year) See Above

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. See Above



### EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsF-2 10/28/2011