FORM A-1

PARENT COMPANY INFORMATION

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 employees 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

FACILITY INFORMATION

II. Facility Information

 Facility Name Johns Manville Waterville Plant 7

 Facility Address

 Street 7500 Dutch Rd.

 City Waterville

 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 Submittal

 Design capacity of the plant (tons/yr) See CBI Submittal

 Type(s) of process(es) (rotary spin, flame attenuation) at this plant Rotary Spin and Flame Attenuation

 Operation schedule

 hrs/day 24

 days/yr 365

 Identify what state and local air pollution rules and regulations, including 

permit requirements, your plant is subject to. (Please provide copies of 

permit(s) and permit IDs) 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, Wound Sliver Product, High Purity Quartz, Felts & 

Quartz

 Are there any HAP emissions associated with any co-located facilities? 

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

We interpret 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

PLANT OPERATIONS

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)

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

 Maximum annual production rate (tons/yr) See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal

 Age of process equipment (yrs) 30 years 30 years 30 years 30 years

 Remaining economic life of process line (yrs)

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/yr; specify year) for each product See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal

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

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

PLANT OPERATIONS

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)

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

 Maximum annual production rate (tons/yr) See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal

 Age of process equipment (yrs) Data Not Available Data Not Available Data Not Available Data Not Available

 Remaining economic life of process line (yrs)

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/yr; specify year) for each product See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal

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

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

PLANT OPERATIONS

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

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

 Maximum annual production rate (tons/yr)

 Age of process equipment (yrs)

 Remaining economic life of process line (yrs)

 List of products produced and most recent annual 

production (tons/yr; 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 Submittal See CBI Submittal See CBI Submittal See CBI Submittal

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 Submittal See CBI Submittal See CBI Submittal See CBI Submittal

See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal

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

PLANT OPERATIONS

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

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

 Maximum annual production rate (tons/yr)

 Age of process equipment (yrs)

 Remaining economic life of process line (yrs)

 List of products produced and most recent annual 

production (tons/yr; 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 Submittal See CBI Submittal

Data Not Available Data Not Available

Indefinite (due to 

rebuild capabilities)

Indefinite (due to 

rebuild capabilities)

See CBI Submittal See CBI Submittal

See CBI Submittal See CBI Submittal

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

PLANT OPERATIONS

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)

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

 Maximum annual production rate (tons/yr) See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal

 Age of process equipment (yrs) Data Not Available Data Not Available Data Not Available Data Not Available

 Remaining economic life of process line (yrs)

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/yr; specify year) for each product See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal

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

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

PLANT OPERATIONS

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

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

 Maximum annual production rate (tons/yr)

 Age of process equipment (yrs)

 Remaining economic life of process line (yrs)

 List of products produced and most recent annual 

production (tons/yr; 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 Submittal See CBI Submittal See CBI Submittal See CBI Submittal

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 Submittal See CBI Submittal See CBI Submittal See CBI Submittal

See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal

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

PLANT OPERATIONS

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

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

 Maximum annual production rate (tons/yr)

 Age of process equipment (yrs)

 Remaining economic life of process line (yrs)

 List of products produced and most recent annual 

production (tons/yr; 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 Submittal See CBI Submittal

Data Not Available Data Not Available

Indefinite (due to 

rebuild capabilities)

Indefinite (due to 

rebuild capabilities)

See CBI Submittal See CBI Submittal

See CBI Submittal See CBI Submittal

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

PLANT OPERATIONS

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)

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

 Maximum annual production rate (tons/yr) See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal

 Age of process equipment (yrs) Data Not Available Data Not Available Data Not Available Data Not Available

 Remaining economic life of process line (yrs)

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/yr; specify year) for each product See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal

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

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

PLANT OPERATIONS

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

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

 Maximum annual production rate (tons/yr)

 Age of process equipment (yrs)

 Remaining economic life of process line (yrs)

 List of products produced and most recent annual 

production (tons/yr; 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 Submittal See CBI Submittal See CBI Submittal See CBI Submittal

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 Submittal See CBI Submittal See CBI Submittal See CBI Submittal

See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal

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

PLANT OPERATIONS

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

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

 Maximum annual production rate (tons/yr)

 Age of process equipment (yrs)

 Remaining economic life of process line (yrs)

 List of products produced and most recent annual 

production (tons/yr; 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 Submittal See CBI Submittal

Data Not Available Data Not Available

Indefinite (due to 

rebuild capabilities)

Indefinite (due to 

rebuild capabilities)

See CBI Submittal See CBI Submittal

See CBI Submittal See CBI Submittal

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

PLANT OPERATIONS

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)

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

 Maximum annual production rate (tons/yr) See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal

 Age of process equipment (yrs) Data Not Available Data Not Available Data Not Available Data Not Available

 Remaining economic life of process line (yrs)

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/yr; specify year) for each product See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal

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

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

PLANT OPERATIONS

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

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

 Maximum annual production rate (tons/yr)

 Age of process equipment (yrs)

 Remaining economic life of process line (yrs)

 List of products produced and most recent annual 

production (tons/yr; 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 Submittal See CBI Submittal See CBI Submittal See CBI Submittal

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 Submittal See CBI Submittal See CBI Submittal See CBI Submittal

See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal

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

PLANT OPERATIONS

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

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

 Maximum annual production rate (tons/yr)

 Age of process equipment (yrs)

 Remaining economic life of process line (yrs)

 List of products produced and most recent annual 

production (tons/yr; 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 Submittal See CBI Submittal

Data Not Available Data Not Available

Indefinite (due to 

rebuild capabilities)

Indefinite (due to 

rebuild capabilities)

See CBI Submittal See CBI Submittal

See CBI Submittal See CBI Submittal

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

PLANT OPERATIONS

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). 1

For each process line: Process Unit 1

 Process line identification names or numbers 2-Meter Melter

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

Melter for making 

glass marbles

 Maximum annual production rate (tons/yr) See CBI Submittal

 Age of process equipment (yrs) Data not available

 Remaining economic life of process line (yrs)

Indefinite (due to 

rebuild capabilities)

 List of products produced and most recent annual 

production (tons/yr; 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

PLANT OPERATIONS

II. Process - Raw materials Handling and Storage

 Molten glass preparation

 Raw materials and proportions by wt (%) Glass Marbles - 100%

 Method(s) of conveying 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 by wt (%) N/A

 List steps in preparing binder, including storage temperature (°F) 

and holding time (hrs) N/A

 Total yearly consumption of binder (gal/yr) N/A

 Cost of binder ($/gal) for most recent year (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

PLANT OPERATIONS

II. Process - Raw materials Handling and Storage

2-Meter Melter 300X Lines

 Molten glass preparation

 Raw materials and proportions by wt (%) See CBI Submittal Glass Marbles - 100%

 Method(s) of conveying 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 by wt (%) 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/yr) N/A N/A

 Cost of binder ($/gal) for most recent year (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

PLANT OPERATIONS

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 (yrs)

Indefinite (due to 

continued 

maintenance)

Indefinite (due to 

continued 

maintenance)

Indefinite (due to 

continued 

maintenance)

Indefinite (due to 

continued 

maintenance)

 Major rebuilds:

 What 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 type: 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 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

 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 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

 Describe process modification(s) since 1999 that reduce 

emissions None None None None

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

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

PLANT OPERATIONS

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 (yrs)

 Major rebuilds:

 What constitues a major rebuild

 Frequency of a major rebuild

 Cost of typical major rebuild

 Date of last major rebuild

 Purpose of last major rebuild

 Increase or decrease in emissions

 Fuel type: electric, gas, or oil 

 Fuel consumption rate (KW/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 

emissions

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 

maintenance)

Indefinite (due to 

continued 

maintenance)

Indefinite (due to 

continued 

maintenance)

Indefinite (due to 

continued 

maintenance)

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 Submittal See CBI Submittal See CBI Submittal See CBI Submittal

See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal

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 Submittal See CBI Submittal See CBI Submittal See CBI Submittal

See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal

None None None None

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

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

PLANT OPERATIONS

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 (yrs)

 Major rebuilds:

 What constitues a major rebuild

 Frequency of a major rebuild

 Cost of typical major rebuild

 Date of last major rebuild

 Purpose of last major rebuild

 Increase or decrease in emissions

 Fuel type: electric, gas, or oil 

 Fuel consumption rate (KW/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 

emissions

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 

maintenance)

Indefinite (due to 

continued 

maintenance)

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 Submittal See CBI Submittal

See CBI Submittal See CBI Submittal

Melting process 

airflow is drawn into 

forming and collection

Melting process 

airflow is drawn into 

forming and collection

See CBI Submittal See CBI Submittal

See CBI Submittal See CBI Submittal

None None

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

EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 P&M Units 1-10 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

 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 (yrs)

Indefinite (due to 

continued 

maintenance)

Indefinite (due to 

continued 

maintenance)

Indefinite (due to 

continued 

maintenance)

Indefinite (due to 

continued 

maintenance)

 Major rebuilds:

 What 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 type: 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 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

 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 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

 Describe process modification(s) since 1999 that reduce 

emissions None None None None

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

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

PLANT OPERATIONS

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 (yrs)

 Major rebuilds:

 What constitues a major rebuild

 Frequency of a major rebuild

 Cost of typical major rebuild

 Date of last major rebuild

 Purpose of last major rebuild

 Increase or decrease in emissions

 Fuel type: electric, gas, or oil 

 Fuel consumption rate (KW/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 

emissions

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 

maintenance)

Indefinite (due to 

continued 

maintenance)

Indefinite (due to 

continued 

maintenance)

Indefinite (due to 

continued 

maintenance)

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 Submittal See CBI Submittal See CBI Submittal See CBI Submittal

See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal

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 Submittal See CBI Submittal See CBI Submittal See CBI Submittal

See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal

None None None None

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

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

PLANT OPERATIONS

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 (yrs)

 Major rebuilds:

 What constitues a major rebuild

 Frequency of a major rebuild

 Cost of typical major rebuild

 Date of last major rebuild

 Purpose of last major rebuild

 Increase or decrease in emissions

 Fuel type: electric, gas, or oil 

 Fuel consumption rate (KW/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 

emissions

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 

maintenance)

Indefinite (due to 

continued 

maintenance)

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 Submittal See CBI Submittal

See CBI Submittal See CBI Submittal

Melting process 

airflow is drawn into 

forming and collection

Melting process 

airflow is drawn into 

forming and collection

See CBI Submittal See CBI Submittal

See CBI Submittal See CBI Submittal

None None

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

EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 P&M Units 11-20 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

 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 (yrs)

Indefinite (due to 

continued 

maintenance)

Indefinite (due to 

continued 

maintenance)

Indefinite (due to 

continued 

maintenance)

Indefinite (due to 

continued 

maintenance)

 Major rebuilds:

 What 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 type: 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 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

 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 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

 Describe process modification(s) since 1999 that reduce 

emissions None None None None

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

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

PLANT OPERATIONS

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 (yrs)

 Major rebuilds:

 What constitues a major rebuild

 Frequency of a major rebuild

 Cost of typical major rebuild

 Date of last major rebuild

 Purpose of last major rebuild

 Increase or decrease in emissions

 Fuel type: electric, gas, or oil 

 Fuel consumption rate (KW/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 

emissions

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 

maintenance)

Indefinite (due to 

continued 

maintenance)

Indefinite (due to 

continued 

maintenance)

Indefinite (due to 

continued 

maintenance)

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 Submittal See CBI Submittal See CBI Submittal See CBI Submittal

See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal

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 Submittal See CBI Submittal See CBI Submittal See CBI Submittal

See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal

None None None None

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

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

PLANT OPERATIONS

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 (yrs)

 Major rebuilds:

 What constitues a major rebuild

 Frequency of a major rebuild

 Cost of typical major rebuild

 Date of last major rebuild

 Purpose of last major rebuild

 Increase or decrease in emissions

 Fuel type: electric, gas, or oil 

 Fuel consumption rate (KW/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 

emissions

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 

maintenance)

Indefinite (due to 

continued 

maintenance)

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 Submittal See CBI Submittal

See CBI Submittal See CBI Submittal

Melting process 

airflow is drawn into 

forming and collection

Melting process 

airflow is drawn into 

forming and collection

See CBI Submittal See CBI Submittal

See CBI Submittal See CBI Submittal

None None

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

EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsB-3 P&M 21-30 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

 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 (yrs)

Indefinite (due to 

continued 

maintenance)

Indefinite (due to 

continued 

maintenance)

Indefinite (due to 

continued 

maintenance)

Indefinite (due to 

continued 

maintenance)

 Major rebuilds:

 What 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 type: 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 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

 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 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

 Describe process modification(s) since 1999 that reduce 

emissions None None None None

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

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:

 Process unit identification name/number

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

 Latitude (decimal degrees, six decimal places)

 Longitude (decimal degrees, six decimal places)

 Stack or vent height (units)

 Stack or vent diameter (units)

 Manufacturer and model

 Date of original installation

 Estimate of remaining lifetime (yrs)

 Major rebuilds:

 What constitues a major rebuild

 Frequency of a major rebuild

 Cost of typical major rebuild

 Date of last major rebuild

 Purpose of last major rebuild

 Increase or decrease in emissions

 Fuel type: electric, gas, or oil 

 Fuel consumption rate (KW/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 

emissions

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 

maintenance)

Indefinite (due to 

continued 

maintenance)

Indefinite (due to 

continued 

maintenance)

Indefinite (due to 

continued 

maintenance)

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 Submittal See CBI Submittal See CBI Submittal See CBI Submittal

See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal

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 Submittal See CBI Submittal See CBI Submittal See CBI Submittal

See CBI Submittal See CBI Submittal See CBI Submittal See CBI Submittal

None None None None

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

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:

 Process unit identification name/number

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

 Latitude (decimal degrees, six decimal places)

 Longitude (decimal degrees, six decimal places)

 Stack or vent height (units)

 Stack or vent diameter (units)

 Manufacturer and model

 Date of original installation

 Estimate of remaining lifetime (yrs)

 Major rebuilds:

 What constitues a major rebuild

 Frequency of a major rebuild

 Cost of typical major rebuild

 Date of last major rebuild

 Purpose of last major rebuild

 Increase or decrease in emissions

 Fuel type: electric, gas, or oil 

 Fuel consumption rate (KW/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 

emissions

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 

maintenance)

Indefinite (due to 

continued 

maintenance)

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 Submittal See CBI Submittal

See CBI Submittal See CBI Submittal

Melting process 

airflow is drawn into 

forming and collection

Melting process 

airflow is drawn into 

forming and collection

See CBI Submittal See CBI Submittal

See CBI Submittal See CBI Submittal

None None

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

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:

 What 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

PLANT OPERATIONS

IV. Process - Forming -- Rotary Spin / Flame Attenuation

 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 Submittal See CBI Submittal See CBI Submittal

 Method of attenuating fiber (e.g., air, flame, or air and flame). 

Indicate type of burner used (if flame). See CBI Submittal See CBI Submittal See CBI Submittal

 Is there a forehearth between the furnace and the forming 

section? No No No

 Major rebuilds:

 What 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.

 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 Submittal See CBI Submittal See CBI Submittal

 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 10/28/2011
 Percent of forming air recirculated and percent exhausted 100% exhausted 100% exhausted 100% exhausted

 Nature and frequency of routine/preventive maintenance 

procedures See CBI Submittal See CBI Submittal See CBI Submittal

 Describe process modification(s) since 1999 that reduce 

emissions None None None

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

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

PLANT OPERATIONS

IV. Process - Forming -- Rotary Spin / Flame Attenuation

 For each Forming Operation -- Rotary Spin/Flame Attenuation

 Process unit identification name/number

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

 Latitude (decimal degrees, six decimal places)

 Longitude (decimal degrees, six decimal places)

 Stack or vent height (units)

 Stack or vent diameter (units)

 Number of fiber forming devices (spinners) per line.

 Method of attenuating fiber (e.g., air, flame, or air and flame). 

Indicate type of burner used (if flame).

 Is there a forehearth between the furnace and the forming 

section?

 Major rebuilds:

 What constitues a major rebuild

 Frequency of a major rebuild

 Cost of typical major rebuild

 Date of last major rebuild

 Purpose of last major rebuild

 Increase or decrease in emissions

 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 Submittal

See CBI Submittal

No

JM is not familiar with 

the term "major 

rebuild." JM conducts 

periodic routine 

maintenace.

N/A

N/A

N/A

N/A

N/A

1

N/A

N/A

N/A

N/A

N/A

Airflow

See CBI Submittal

Approx. 32,000 acfm at 

85 °F per APC unit

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

 Nature and frequency of routine/preventive maintenance 

procedures

 Describe process modification(s) since 1999 that reduce 

emissions

 Describe future source reduction plans and schedules

100% exhausted

See CBI Submittal

None

See CBI Submittal

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

PLANT OPERATIONS

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:

 What constitues a major rebuild

 Frequency of a major rebuild

 Cost of typical major rebuild

 Date of last major rebuild

 Purpose of last major rebuild

 Increase or decrease in emissions

 Fuel type: electric, gas, or oil 

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

 Moisture content wt (%) of formed mat: 

 inlet

 outlet

 Air flow rate (acfm @ °F) from curing

 Exhaust air temperature (°F)

 Residence time of product (mins)

 Binder content of cured product (LOI)

 Nature and frequency of routine/preventive 

maintenance procedures

 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

PLANT OPERATIONS

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 

maintenance 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

PLANT OPERATIONS

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. We interpret this question to apply to wool 

fiberglass lines, from melting through cooling. None

 List each solvent used and quantity (gal/yr) 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 OPERATIONS

VIII. Pollution Prevention

Please describe any work practices, pollution prevention techniques, 

and control strategies evaluated and/or implemented at each process 

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

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

You must specify the year in which the facility implemented the 

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

from these practices/techniques.

JM objects to this question in that it is unbounded in time. 

We interpret this question, like similar questions in the 

ICR, to seek data since 1999. With that interpretation, JM 

responds that there have been none.

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

AIR POLLUTION CONTROL

I. Electrostatic Precipitator (ESP) N/A

 For each ESP: ESP 1 ESP 2 ESP 3

 Process line(s) (identification name/number)

 Equipment/process(es) controlled. Include emission point 

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

 Latitude (decimal degrees, six decimal places)

 Longitude (decimal degrees, six decimal places)

 Stack or vent height (units)

 Stack or vent diameter (units)

 Manufacturer and model

 Date of original installation

 Number of collection plates and configuration

 Gas flow rate to ESP (acfm @ °F)

 Inlet gas temperature (°F)

 Outlet gas temperature (°F)

 Inlet grain loading (gr/dscf)

 Outlet grain loading (gr/dscf)

 Average stack opacity (%)

 Pressure drop across ESP (in. H

2O gauge)

 Plate area (ft

2

)

 Vendor guarantee on ESP 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/yr)

 Quantity of solid waste disposed of (lbs/yr)

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

 Nature and frequency of routine/preventive maintenance 

procedures

 Problems experienced with control device within the last five 

years; how were problems solved?

 Continuous monitoring method(s) used to monitor ESP 

performance, including parameters monitored

 Describe any plans to replace or upgrade ESP

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

AIR 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

 Equipment/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

 Type (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

 Water 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 Water Softened City Water Softened City Water

 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) Ambient Ambient Ambient

 Liquid/gas ratio (gal/103 acfm) ~ 1.43 gal/103 acfm ~ 1.43 gal/103 acfm ~ 1.43 gal/103 acfm

 Pressure drop across scrubber (in. H2O 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/yr) 0 0 0

EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsC-2 10/28/2011
 Quantity of solid waste disposed of (lbs/yr) 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, 

maintenance performed as 

needed

Scrubber are cleaned out 

once per year, 

maintenance performed as 

needed

Scrubber are cleaned out 

once per year, 

maintenance performed as 

needed

 Problems experienced with control device within the last five years; 

how were problems 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 Submittal See CBI Submittal See CBI Submittal

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

AIR POLLUTION CONTROL

II. Scrubber

 For each Scrubber:

 Process line(s) (identification name/number)

 Equipment/process(es) controlled. Include emission point 

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

 Latitude (decimal degrees, six decimal places)

 Longitude (decimal degrees, six decimal places)

 Stack or vent height (units)

 Stack or vent diameter (units)

 Manufacturer and model

 Date of original installation

 Type (e.g., venturi, orifice)

 Gas flow rate to scrubber (acfm @ °F)

 Inlet gas temperature (°F)

 Outlet gas temperature (°F)

 Inlet grain loading (gr/dscf)

 Outlet grain loading (gr/dscf)

 Average stack opacity (%)

 Water flow rate to scrubber (gpm)

 Percent of scrubber water from recycled wastewater

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

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

 HAP composition of wastewater (mg/L)

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

scrubbing water

 Scrubbing water temperature (°F)

 Liquid/gas ratio (gal/103 acfm)

 Pressure drop across scrubber (in. H2O gauge)

 Amount of wastewater generated (gpd)

 Amount of wastewater recycled (gpd)

 Amount of wastewater disposed of (gpd)

 Method of wastewater disposal

 Quantity of solid waste collected (lbs/yr)

 Quantity of solid waste recycled (lbs/yr)

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 Water Softened City Water Softened City Water

None known None known None known

No data available No data available No data available

Ambient Ambient Ambient

 ~ 1.43 gal/103 acfm ~ 1.43 gal/103 acfm ~ 1.43 gal/103 acfm

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 10/28/2011
 Quantity of solid waste disposed of (lbs/yr)

 Method of solid waste disposal

 Vendor guarantee on scrubber efficiency (attach copy)

 Nature and frequency of preventive maintenance procedures

 Problems experienced with control device within the last five years; 

how were problems solved?

 Continuous monitoring method(s) used to monitor scrubber 

performance, including parameters monitored

 Plans to replace or upgrade scrubber

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, 

maintenance performed as 

needed

Scrubber are cleaned out 

once per year, 

maintenance performed as 

needed

Scrubber are cleaned out 

once per year, 

maintenance 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 Submittal See CBI Submittal See CBI Submittal

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

AIR POLLUTION CONTROL

III. Mechanical Collector

 For each Mechanical Collector: Mechanical Collector 1

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

 Equipment/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

 Type of mechanical collector 

Wire 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. H2O 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/yr) 0

 Quantity of solid waste disposed of (lbs/yr) 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 

years; 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 10/28/2011
 Plans to replace or upgrade mechanical collector See CBI Submittal

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

AIR POLLUTION CONTROL

IV. Fabric Filter 

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

 Process line(s) (identification name/number) Osprey 61 Osprey 62 Osprey 63

 Equipment/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. H2O 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/yr) 0 0 0

 Quantity of solid waste disposed of (lbs/yr) 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 10/28/2011
 Problems 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 Submittal See CBI Submittal See CBI Submittal

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

AIR POLLUTION CONTROL

IV. Fabric Filter 

 For each Fabric Filter:

 Process line(s) (identification name/number)

 Equipment/process(es) controlled. Include emission 

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

 Latitude (decimal degrees, six decimal places)

 Longitude (decimal degrees, six decimal places)

 Stack or vent height (units)

 Stack or vent diameter (units)

 Manufacturer and model

 Date of original installation

 Number of compartments

 Number of bags per compartment

 Filter material and coatings applied

 Fabric weight (oz/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. H2O gauge)

 Method and frequency of bag cleaning

 Vendor guarantee on fabric filter efficiency (attach 

copy)

 Quantity of solid waste collected (lbs/yr)

 Quantity of solid waste recycled (lbs/yr)

 Quantity of solid waste disposed of (lbs/yr)

 Method of solid waste disposal

 Nature and frequency of preventive maintenance 

procedures

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 10/28/2011
 Problems experienced with control device within the 

last five years; how were problems solved?

 Continuous monitoring method(s) used to monitor 

performance, including parameters monitored

 Plans to replace or upgrade fabric filter

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 Submittal See CBI Submittal See CBI Submittal

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

AIR POLLUTION CONTROL

IV. Fabric Filter 

 For each Fabric Filter:

 Process line(s) (identification name/number)

 Equipment/process(es) controlled. Include emission 

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

 Latitude (decimal degrees, six decimal places)

 Longitude (decimal degrees, six decimal places)

 Stack or vent height (units)

 Stack or vent diameter (units)

 Manufacturer and model

 Date of original installation

 Number of compartments

 Number of bags per compartment

 Filter material and coatings applied

 Fabric weight (oz/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. H2O gauge)

 Method and frequency of bag cleaning

 Vendor guarantee on fabric filter efficiency (attach 

copy)

 Quantity of solid waste collected (lbs/yr)

 Quantity of solid waste recycled (lbs/yr)

 Quantity of solid waste disposed of (lbs/yr)

 Method of solid waste disposal

 Nature and frequency of preventive maintenance 

procedures

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 10/28/2011
 Problems experienced with control device within the 

last five years; how were problems solved?

 Continuous monitoring method(s) used to monitor 

performance, including parameters monitored

 Plans to replace or upgrade fabric filter

Data Not Available

None

See CBI Submittal

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

AIR 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)

 Equipment/process(es) controlled. Include emission 

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

 Latitude (decimal degrees, six decimal places)

 Longitude (decimal degrees, six decimal places)

 Stack or vent height (units)

 Stack or vent diameter (units)

 Manufacturer and model

 Date of original installation

 Fuel type: 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

AIR POLLUTION CONTROL

VI. High Velocity Air Filter (HVAF) N/A

 For each HVAF: HVAF 1 HVAF 2 HVAF 3

 Process line(s) (identification name/number)

 Equipment/process(es) controlled. Include emission 

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

 Latitude (decimal degrees, six decimal places)

 Longitude (decimal degrees, six decimal places)

 Stack or vent height (units)

 Stack or vent diameter (units)

 Manufacturer and model

 Date of original installation

 Inlet gas flow rate (acfm @ °F)

 Inlet gas temperature (°F)

 Outlet gas temperature (°F)

 Inlet grain loading (gr/dscf)

 Outlet grain loading (gr/dscf)

 Average stack opacity (%)

 Water spray pressure (sdig), if applicable

 Water spray rate (gpm), if applicable

 Filter face velocity (acfm/ft

2

)

 Maximum pressure drop across mat (in. H

2O gauge)

 Vendor guarantee on HVAF efficiency (attach copy)

 Method and frequency of filter mad advancement

 Amount of wastewater generated (gpd)

 Amount of wastewater recycled (gpd)

 Amount of wastewater disposed of (gpd)

 Method of wastewater disposal

 Quantity of solid waste collected (lbs/yr)

 Quantity of solid waste recycled (lbs/yr)

 Quantity of solid waste disposed of (lbs/yr)

 Method of solid waste disposal

 Nature and frequency of preventive maintenance 

procedures

EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsC-6 10/28/2011
 Problems experienced with control device within the 

last five years; how were problems solved?

 Continuous monitoring method(s) used to monitor 

HVAF performance, including parameters monitored

 Plans to replace or upgrade HVAF

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

AIR 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)

 Equipment/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

 Type of mist eliminator

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

 Inlet gas temperature (°F)

 Outlet gas temperature (°F)

 Inlet grain loading (gr/dscf)

 Outlet grain loading (gr/dscf)

 Average stack opacity (%)

 Velocity in mist eliminator (ft/sec)

 Pressure drop (in. H2O gauge)

 For chevron blade mist eliminators:

 Spacing between blades (in.)

 Washing frequency of blades

 For mesh pad mist eliminators:

 Number of pads or elements

 Thickness of pad (in.) or element dimensions

 Density of pad, (lb/ft3)

 Washing frequency of pad

 Vendor guarantee on mist eliminator efficiency (attach copy)

 Amount of wastewater generated (gpd)

 Amount of wastewater recycled (gpd)

 Amount of wastewater disposed of (gpd)

 Method of wastewater disposal

 Quantity of solid waste collected (lbs/yr)

 Quantity of solid waste recycled (lbs/yr)

EPA-HQ-OAR-2010-1042-DRAFT-0002.xlsC-7 10/28/2011
 Quantity of solid waste disposed of (lbs/yr)

 Method of solid waste disposal

 Nature and frequency of preventive maintenance procedures

 Problems experienced with control device within the last five 

years; how were problems solved?

 Continuous monitoring method(s) used to monitor mist eliminator 

performance, including parameters monitored

 Plans to replace or upgrade mist eliminator 

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

AIR 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)

 Equipment/process(es) controlled. Include emission point 

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

 Latitude (decimal degrees, six decimal places)

 Longitude (decimal degrees, six decimal places)

 Stack or vent height (units)

 Stack or vent diameter (units)

 For general or building ventilation:

 Ventilation system used

 Airflow control system used

 Number of air changes per hour

 For unit or local ventilation:

 Enclosure or hood design used

 Volume of enclosure or hood

 Capture velocity (ft/sec)

 Distance between hood and emission source (ft)

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

AIR 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)

 Equipment/process(es) controlled. Include emission point 

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

 Latitude (decimal degrees, six decimal places)

 Longitude (decimal degrees, six decimal places)

 Stack or vent height (units)

 Stack or vent diameter (units)

 Description

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

PROCESS LINE STARTUP AND 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 

emissions source or sources associated with the startup or 

shutdown; N/A

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

permit condition was exceeded; N/A

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

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

whether the plan was followed; if the plan was not followed, why not; 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. Whether the emission profile of each unit was different during 

startup and shutdown than during normal operating conditions and, if 

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

supporting information; 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 

monitoring, collected during each period of SS. All 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 10/28/2011
If this information is contained in periodic and immediate SS reports 

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

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

of those reports instead.

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

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

explain how these events were eliminated. 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 monitoring data, including control system 

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

years. 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 minimize 

emissions 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 AIR POLLUTANTS IN EMISSION POINTSa

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 emissions data.

Melting 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 

matter, 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, carbonyl sulfide, hydrogen fluoride, metals 

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

selenium), mercury, and hexavalent chromium. The scope of the existing data provided 

was the result of consensus reached by EPA, NAIMA, and industry representatives. In 

addition to the existing 

data submitted to EPA, extensive new emissions data is being collected from 

virtually all companies through the “BTEC, Inc. Quality Assurance Project Plan for 

the Mineral Wool and Wool Fiberglass Emissions Test Program.” This Test Program

will collect and submit to EPA, through EPA’s Electronic Reporting Tool, 

representative emissions data for the following pollutants: formaldehyde, methanol, 

phenol, particulate matter, carbon monoxide, carbonyl sulfide, hydrogen fluoride, 

metals (antimony, arsenic, beryllium, cadmium, chromium, cobalt, lead, manganese, 

nickel, and selenium), mercury, and hexavalent chromium.

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 

Administrator’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. Annual 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 materials 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 

Water See Above 

 Waste 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 10/28/2011
 Other (specify) warewhouse allocation, general plant allocation, and 

employee 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 

your 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 

most 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. Air Pollution Control Device (APCD) 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 

Administrator’s review 

obligations pursuant to 

Clean Air Act Section 

112(d)(6) and 112(f)(2).

 APCD equipment purchase cost and what was included See Above 

 List the cost for each piece of auxiliary equipment 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. Annual Operating Costs

 Base year (most recent fiscal year) See Above 

 Maintenance materials and replacement parts (specify costs by

item) See Above 

 Raw materials 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 

 Waste treatment and/or disposal See Above 

 Indirect costs See Above 

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