### FORM A**-1**

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

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

1. Legal Parent Company / Legal Corporate Name United States Mineral Products Company dba Isolatek International 2. Address 41 Furnace Street 3. City Stanhope 4. State NJ 5. Zip Code 07874 6. County Sussex 7. Size of Company (approximate number of employees including all subsidiaries, branches, and related establishments owned): 162**FORM A -2** 

**FA CILITY INFORMA** 

**TI ON** 

**II. Facility Information**

Facility Name Isolatek International Facility Address Street 701 North Broadway City Huntington State IN Zip Code 46750 County Huntington Facility Coordinates Latitude (decimal degrees, six decimal places) 40.887187 Longitude (decimal degrees, six decimal places) -85.467957 Specific location represented (e.g., front door of main building, centroid of property, etc.) Cupola Baghouse Stack

**Number of employees attached to the mineral wool production facility:**  **Will be submitted as Confidential Business Proprietary Information (CBI)**

**Design capacity of the plant (tons/yr) Will be submitted as Confidential Business Proprietary Information (CBI)** 

Type(s) of process(es) (rotary spin, flame attenuation) at this plant 4 wheel spinner

Operation schedule hrs/day 24 days/yr 300

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) IDEM Operation Permit No.: T 069-18676-00021

**III. T echnical Contact** 

Name Tom Lund Technical Contact Title Operations Manager Telephone (260) 356-2040 x328 Facsimile (Fax) (260) 356-2337 Email tlund@isolatek.com

**IV. Other**

Is the facility a major source of HAP? Ye s
If "No", did the facility take a limit of its potential HAP emissions to avoid classification as a major source?

Does the facility manufacture other products in addition to mi neral wool? No. All products use bulk (loose) mineral wool as the base ingredient.

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

Are there any HAP emissions associated with any co-located facilities? List unit operations, e.g., boiler, and pollutant/emissions

### FORM B-1

**PLA NT OPERA** 

**TIONS**

**I. Overview of Process Operations**

Number of process lines. Include lines that are currently operational or that are temporarily shutdown. (Do not include lines permanently shutdown). 2

For each process line: Process Line 1 Process Line 2 Process line identification name or numbers 1 2 Ty pe of process line (e.g., Fiberization method) 4 wheel spinner 4 wheel spinner

**Maximum annual production rate (tons/yr) Will be submitted as Confidential**  **Business Proprietary Information (CBI)**  **Will be submitted as Confidential Business**  **Proprietary Information (CBI)** Age of process line (y rs) >25 >25 Remaining economic life of process line (y rs)

**List of products produced and most recent annual production (tons/yr; specify year) for each product**  **Will be submitted as Confidential Business Proprietary**  **Information (CBI) Will be submitted as**  **Confidential Business Proprietary Information (CBI)** 

**Please attach detailed schematics of each process line.**  **Will be submitted as Confidential Business Proprietary**  **Information (CBI)**

### Will be submitted as Confidential Business Proprietary Information (CBI)

### FORM B-2

**PROCESS OPERA TIONS** 

**II. Raw Material Handling and Storage**

Cupola charge preparation

**Raw materials and proportions by wt (%) Will be submitted as Confidential Business Proprietary**  **Information (CBI)** Method(s) of convey ing each raw material to cupola Charge Bucket Binder and Additives List each raw material, including premixed materials, in the binder formulation and its proportion bywt (%) N/A List steps in preparing binder, including storage temperature (° F) and holding time (hrs) N/A Total yearly

consumption of binder, excluding water, (gal/y r) N/A Cost of binder, excluding water, ($/gal) for most recent
ye ar (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

### Will be submitted as Confidential Business Proprietary Information (CBI)**FORM B-3**

**PROCESS OPERATIONS**

**III. Cupola/furnace**

For each cupola: Cupola 1 Cupola 2 Process unit identification name/number 1 2 Process line(s) served (identification name/number) 1 2 Latitude (decimal degrees, six decimal places) 40.887296 40.88725 Longitude (decimal degrees, six decimal places) -85.468287 -85.468273 Stack or vent height (units) 49' 49' Stack or vent diameter (units) 4' 4' Manufacturer and model USM Design USM Design Date of original installation 1983 1985 Estimate of remaining lifetime (yrs) N/A N/A Major rebuilds:

W hat constitues a major rebuild Frequency of a major rebuild N/A N/A Cost of typical major rebuild N/A N/A Date of last major rebuild N/A N/A Purpose of last major rebuild N/A N/A Increase or decrease in emissions N/A N/A Fuel type: coke, electric, gas, or oil Coke Coke

**Fuel consumption rate (Btu/ton of melt) Will be submitted as**  **Confidential Business Proprietary Information**  **(CBI) Will be submitted as**  **Confidential Business Proprietary Information**  **(CBI)**

**Design production rate (tons/day) Will be submitted as**  **Confidential Business Proprietary Information**  **(CBI) Will be submitted as**  **Confidential Business Proprietary Information**  **(CBI)**

**Actual glass pull rate (tons/day) - melt rate Will be submitted as**  **Confidential Business Proprietary Information**  **(CBI) Will be submitted as**  **Confidential Business Proprietary Information**  **(CBI)** Exhaust air flow rate (acfm @ ° F) 3500 3500 Temperature (° F) of melt as it exits the cupola 2200 2200

Is oxygen enrichment used to supplement combustion air Yes Yes **Quantity of oxygen supplied for enrichment (cu. ft. O2/ton coke)**  **Will be submitted as Confidential Business**  **Proprietary Information (CBI)**  **Will be submitted as Confidential Business**  **Proprietary Information (CBI)**  Nature and frequency of routine/preventive maintenance procedures 7 days 7 days

Describe process modification(s) since 1999 that reduce emissions

Describe future source reduction plans and schedules N/A N/A 2002 - Install heat exchanger and use exhaust air to heat combustion air (reduce coke usage)

2005 - Oxygen enrichment to reduce coke usage.

2009 - Insulate the cupola hood to reduce coke usage. Isolatek will undertake routine cupola repair projects as needed. These projects do not impact the cupola emissions, and therefore are not considered major rebuilds for the purpose of this ICR.

### FORM B-4

**PROCESS OPERA**

**TIONS**

**IV. Fiberization**

For each fiberization operation: Fiberization Operation 1 Fiberization Operation 2 Fiberization Operation 3 Process unit identification name/number N/A - Non-Bonded Process line(s) served (identification name/number) N/A - Non-Bonded Latitude (decimal degrees, six decimal places) N/A - Non-Bonded Longitude (decimal degrees, six decimal places) N/A - Non-Bonded Stack or vent height (units) N/A - Non-Bonded Stack or vent diameter (units) N/A - Non-Bonded Number of fiber forming devices (spinners) per line N/A - Non-Bonded Method of attenuation fiber (air, centrifical force, or both) N/A - Non-Bonded Major rebuilds: W hat constitutes a major rebuild N/A - Non-Bonded Frequency of a major rebuild N/A - Non-Bonded Cost of typical major rebuild N/A - Non-Bonded Date of last major rebuild N/A - Non-Bonded Purpose of last major rebuild N/A - Non-Bonded Increase or decrease in emissions N/A - Non-Bonded If forming section is modular, i.e., more than one forming and collection area per line, indicate the number of modules and air plenums. N/A - Non-Bonded Presence of water overspray and application range (gpm) N/A - Non-Bonded Binder applied and application rate (gpm) N/A - Non-Bonded Other material applied (annealing oil or oil/water emulsion) and application rate (gpm) N/A - Non-Bonded Temperature of binder when applied to the fibers ( ° F) N/A - Non-Bonded Forming air flow rate (acfm @ °F) N/A - Non-Bonded

Percent of forming air recirculated and percent exhausted N/A - Non-Bonded Nature and frequency of routine/preventive maintenance procedures N/A - Non-Bonded Describe process modification(s) since 1999 that reduce emissions N/A - Non-Bonded Describe future source reduction plans and schedules N/A - Non-Bonded Fiberization method (e.g., Downey process or Yo uger/Powell process) N/A - Non-Bonded Number of rotors N/A - Non-Bonded Configuration of rotor(s) N/A - Non-Bonded Amount of material that remains non-fiberized shot N/A - Non-Bonded Exhaust air flow rate (acfm @ ° F) N/A - Non-Bonded

### FORM B-5

**PROCESS OPERA**

**TIONS**

**V. Fiber Collection**

For each fiber collection operation: Fiber Collection Operation 1 Fiber Collection Operation 2 Fiber Collection Operation 3 Process unit identification name/number N/A - Non-Bonded Process line(s) served (identification name/number) N/A - Non-Bonded Latitude (decimal degrees, six decimal places) N/A - Non-Bonded Longitude (decimal degrees, six decimal places) N/A - Non-Bonded Stack or vent height (units) N/A - Non-Bonded Stack or vent diameter (units) N/A - Non-Bonded Method of fiber collection from fiberization N/A - Non-Bonded Manufacturer and model of collection chamber N/A - Non-Bonded Date of original installation N/A - Non-Bonded Major rebuilds: W hat constitutes a major rebuild N/A - Non-Bonded Frequency

of a major rebuild N/A - Non-Bonded Cost of typical major rebuild N/A - Non-Bonded Date of last major rebuild N/A - Non-Bonded Purpose of last major rebuild N/A - Non-Bonded Increase or decrease in emissions N/A - Non-Bonded

Air flow rate (acfm @ ° F) in pneumatic fiber convey ing N/A - Non-Bonded Exhaust air flow rate (acfm @ °F) N/A - Non-Bonded Residence time of product (mins) (time spent in collection device) N/A - Non-Bonded

Method of evenly

distributing fibers onto conveyor belt N/A - Non-Bonded Formed mat thickness (in.) N/A - Non-Bonded Nature and frequency of routine/preventive

ma intenance procedures N/A - Non-Bonded Describe process modification(s) since 1999 that reduce emissions N/A - Non-Bonded

Describe future source reduction plans and schedules N/A - Non-Bonded

### FORM B-6

**PROCESS OPERA**

**TIONS**

**VI. Curing**

For each curing oven: Curing Oven 1 Curing Oven 2 Curing Oven 3 Process unit identification name/number N/A Process line(s) served (identification name/number) N/A Latitude (decimal degrees, six decimal places) N/A Longitude (decimal degrees, six decimal places) N/A Stack or vent height (units) N/A Stack or vent diameter (units) N/A Method of curing N/A Manufacturer and model N/A Date of original installation N/A Major rebuilds: W hat constitutes a major rebuild N/A Frequency

of a major rebuild N/A Cost of typical major rebuild N/A Date of last major rebuild N/A Purpose of last major rebuild N/A Increase or decrease in emissions N/A Fuel ty pe: electric, gas, or oil N/A Fuel consumption rate (KW /hr or BTU/hr) N/A Curing temperature (° F) N/A Moisture content wt (%) of formed mat: inlet N/A outlet N/A Exhaust air flow rate (acfm @ ° F) from curing N/A Residence time of product (mins) N/A Binder content of cured product (LOI) N/A Nature and frequency of routine/preventive maintenance procedures N/A Describe process modification(s) since 1999 that reduce

em issions N/A Describe future source reduction plans and schedules N/A

### FORM B-7

**PROCESS OPERA**

**TIONS**

**VII. Cooling**

For each cooling operation: Cooling Operation 1 Cooling Operation 2 Cooling Operation 3 Process unit identification name/number 

### N/A Process line(s) served (identification name/number) 

### N/A Latitude (decimal degrees, six decimal places) 

### N/A Longitude (decimal degrees, six decimal places) 

### N/A Stack or vent height (units) 

### N/A Stack or vent diameter (units) 

### N/A Cooling air flow rate (acfm @ ° F) 

### N/A Percentage of cooling air recirculated (if any) 

### N/A Cooling air temperature (°F) 

### N/A Exhaust air flow rate (acfm @ °F) 

### N/A Nature and frequency of routine/preventive maintenance procedures 

### N/A Describe process modification(s) since 1999 that reduce

em issions 

### N/A Describe future source reduction plans and schedules 

### N/A

### FORM B-8

**PROCESS OPERA**

**TIONS**

**VIII. Pollution Prevention**

**Please describe any work practices, pollution prevention techniques, and control strategies evaluated and/or implemented**  **at each process unit at your facility (e.g., binder reformulation, alternative fuels usage, etc.) to reduce emissions of PM, CO, and**  **HA Ps 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. Heat Exchanger to reduce coke - 2003**  **Insulate hood to reduce coke - 2009 FORM C-1** 

**AIR POLLUTION CONTROL**

**I. Electrostatic Precipitator (ESP)**

For each ESP: ESP 1 ESP 2 ESP 3 Process line(s) (identification name/number) N/A Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan) N/A Latitude (decimal degrees, six decimal places) N/A Longitude (decimal degrees, six decimal places) N/A Stack or vent height (units) N/A Stack or vent diameter (units) N/A Manufacturer and model N/A Date of original installation N/A Number of collection plates and configuration N/A Gas flow rate to ESP (acfm @ ° F) N/A Inlet gas temperature (° F) N/A Outlet gas temperature (° F) N/A Inlet grain loading (gr/dscf) N/A Outlet grain loading (gr/dscf) N/A Average stack opacity (%) N/A Pressure drop across ESP (in. H 2 O gauge) N/A Plate area (ft2 ) N/A Vendor guarantee on ESP efficiency (attach copy) N/A Method of plate cleaning and frequency N/A Flow rate of plate wash water to ESP (gpm), if applicable N/A Temperature of plate wash water to ESP (° F), if applicable N/A Source of plate wash water used for cleaning, if applicable N/A Concentration (mg/l) of dissolved and suspended solids in plate wash water, if applicable N/A Conditioning agents used and amounts (in gpm or lbs/hr), if applicable N/A Amount of wastewater generated (gpd), if applicable N/A Amount of wastewater recycled (gpd), if applicable N/A Amount of wastewater disposed of (gpd), if applicable N/A Method of wastewater disposal, if applicable N/A Quantity of solid waste collected (lbs/yr) N/A Quantity of solid waste recycled (lbs/yr) N/A Quantity of solid waste disposed of (lbs/yr) N/A Method of solid waste disposal N/A Nature and frequency of routine/preventive maintenance procedures N/A Problems experienced with control device within the last five ye ars; how were problems solved? N/A Continuous monitoring method(s) used to monitor ESP performance, including parameters monitored N/A Describe any plans to replace or upgrade ESP N/A**FORM C-2**

**AIR POLLUTION CONTROL**

**II. Scrubber**

For each scrubber: Scrubber 1 Scrubber 2 Scrubber 3 Process line(s) (identification name/number) N/A Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan) N/A Latitude (decimal degrees, six decimal places) N/A Longitude (decimal degrees, six decimal places) N/A Stack or vent height (units) N/A Stack or vent diameter (units) N/A Manufacturer and model N/A Date of original installation N/A Type (e.g., venturi, orifice) N/A Gas flow rate to scrubber (acfm @ ° F) N/A Inlet gas temperature (° F) N/A Outlet gas temperature (° F) N/A Inlet grain loading (gr/dscf) N/A Outlet grain loading (gr/dscf) N/A Average stack opacity (%) N/A W ater flow rate to scrubber (gpm) N/A Percent of scrubber water from recycled wastewater N/A

Source of scrubbing water and type of pretreatment. Substance(s) added as part of pretreatment and amount used (gpm or lbs/hr) N/A HAP composition of wastewater (mg/L) N/A Concentration (mg/L) of dissolved and suspended solids in scrubbing water N/A Scrubbing water temperature (° F) N/A Liquid/gas ratio (gal/10 3acfm) N/A Pressure drop across scrubber (in. H 2 O gauge) N/A Amount of wastewater generated (gpd) N/A Amount of wastewater recycled (gpd) N/A Amount of wastewater disposed of (gpd) N/A Method of wastewater disposal N/A Quantity of solid waste collected (lbs/yr) N/A Quantity of solid waste recycled (lbs/yr) N/A Quantity of solid waste disposed of (lbs/yr) N/A Method of solid waste disposal N/A Vendor guarantee on scrubber efficiency (attach copy) N/A Nature and frequency of preventive maintenance procedures N/A Problems experienced with control device within the last five years; how were problems solved? N/A Continuous monitoring method(s) used to monitor scrubber performance, including parameters monitored N/A Plans to replace or upgrade scrubber N/A

### FORM C-3

**AI R POLLUTION CONTROL** 

**III. Mechanical Collector**

For each mechanical collector: Mechanical Collector 1 Mechanical Collector 2 Mechanical Collector 3 Process line(s) (identification name/number) 

### N/A Equipm ent/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan) 

### N/A Latitude (decimal degrees, six decimal places) 

### N/A Longitude (decimal degrees, six decimal places) 

### N/A Stack or vent height (units) 

### N/A Stack or vent diameter (units) 

### N/A Manufacturer and model 

### N/A Date of original installation 

### N/A Ty pe of mechanical collector 

### N/A Gas flow rate to collector (acfm @ ° F) 

### N/A Inlet gas temperature (° F) 

### N/A Outlet gas temperature (° F) 

### N/A Inlet grain loading (gr/dscf) 

### N/A Outlet grain loading (gr/dscf) 

### N/A Average stack opacity (%) 

### N/A Overall pressure drop (in. H 2 

### O gauge) 

### N/A Vendor guarantee on mechanical collector efficiency (attach copy) 

### N/A Quantity

of solid waste collected (lbs/y r) 

### N/A Quantity

of solid waste recycled (lbs/y r) 

### N/A Quantity

of solid waste disposed of (lbs/y r) 

### N/A Method of solid waste disposal 

### N/A

Nature and frequency of preventive maintenance procedures 

### N/A Problems experienced with control device within the last five ye ars; how were problems solved? 

### N/A Continuous monitoring method(s) used to monitor performance, including parameters monitored 

### N/A Plans to replace or upgrade mechanical collector 

### N/A**FORM C-4**

**AIR POLLUTION CONTROL**

**IV. Fabric Filter**

For each fabric filter: Fabric Filter 1 Process line(s) (identification name/number) 

### 1 & 2 Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan) 

### Cupola 1 (EU1) Cuopla 2 (EU2) Latitude (decimal degrees, six decimal places) 40.887219 Longitude (decimal degrees, six decimal places) -85.467949 Stack or vent height (units) 49' Stack or vent diameter (units) 4' Manufacturer and model 

### Dustex Date of original installation 

### 2002 Number of compartments 

### 4 Number of bags per compartment 

### 120 Filter material and coatings applied 

### Aramid Felt Fabric weight (oz/yd 2 ) 

### 14 Filter surface area (ft2 ) 

### 9360 Gas flow rate to filter (acfm @ ° F) 

### 32620 Inlet gas temperature (° F) 

### 350 Outlet gas temperature (° F) 

### 255 Inlet grain loading (gr/dscf) 

### Unknown Outlet grain loading (gr/dscf) 

### 0.0008 Average stack opacity (%) 

### 0 Overall pressure drop (in. H 2 O gauge) 

### 10

Method and frequency of bag cleaning 

### Pressure >10in H2O or every 15 minutes Vendor guarantee on fabric filter efficiency (attach copy) 

### N/A Quantity of solid waste collected (lbs/yr) 

### 86400000 Quantity of solid waste recycled (lbs/yr) 

### 0 Quantity of solid waste disposed of (lbs/yr) 

### 86400000 Method of solid waste disposal 

### land fill Nature and frequency of preventive maintenance procedures 

### bi-weekly, inspect bags Problems experienced with control device within the last five ye ars; how were problems solved? 

### none

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

### Broken Bag Alarm Pressure Drop Visible Emissions Plans to replace or upgrade fabric filter 

### none

### FORM C-5

**AI R POLLUTION CONTROL** 

**V. Thermal Incinerator**

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

### N/A Equipm ent/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan) 

### N/A Latitude (decimal degrees, six decimal places) 

### N/A Longitude (decimal degrees, six decimal places) 

### N/A Stack or vent height (units) 

### N/A Stack or vent diameter (units) 

### N/A Manufacturer and model 

### N/A Date of original installation 

### N/A Fuel ty pe: gas or oil 

### N/A Fuel consumption rate (BTU/hr) 

### N/A Inlet gas flow rate (acfm @ ° F) 

### N/A Inlet gas temperature (° F) 

### N/A Combustion chamber gas temperature (° F) 

### N/A Outlet gas temperature (° F) 

### N/A Inlet grain loading (gr/dscf) 

### N/A Outlet grain loading (gr/dscf) 

### N/A Average stack opacity (%) 

### N/A Excess air (%) 

### N/A Residence time (sec) at temperature (° F) 

### N/A Percent heat recovery 

### N/A Vendor guarantee on incinerator efficiency (attach copy) 

### N/A

Nature and frequency of preventive maintenance procedures 

### N/A Problems experienced with control device within the last five ye ars; how were problems solved? 

### N/A Continuous monitoring method(s) used to monitor incinerator performance, including parameters monitored 

### N/A Plans to replace or upgrade thermal incinerator 

### N/A**FORM C-6**

**AI R POLLUTION CONTROL** 

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

For each HVAF: HVAF 1 HVAF 2 HVAF 3 Process line(s) (identification name/number) N/A Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan) N/A Latitude (decimal degrees, six decimal places) N/A Longitude (decimal degrees, six decimal places) N/A Stack or vent height (units) N/A Stack or vent diameter (units) N/A Manufacturer and model N/A Date of original installation N/A Inlet gas flow

rate (acfm @ ° F) N/A Inlet gas temperature ( ° F) N/A Outlet gas temperature ( ° F) N/A Inlet grain loading (gr/dscf) N/A Outlet grain loading (gr/dscf) N/A Average stack opacity (%) N/A W ater spray pressure (psig), if applicable N/A W ater spray rate (gpm), if applicable N/A Filter face velocity (acfm/ft 2 ) N/A Maximum pressure drop across mat (in. H 2 O gauge) N/A Vendor guarantee on HVAF efficiency (attach copy) N/A Method and frequency of filter mad advancement N/A Amount of wastewater generated (gpd) N/A Amount of wastewater recycled (gpd) N/A Amount of wastewater disposed of (gpd) N/A Method of wastewater disposal N/A Quantity of solid waste collected (lbs/yr) N/A Quantity of solid waste recycled (lbs/yr) N/A Quantity of solid waste disposed of (lbs/yr) N/A Method of solid waste disposal N/A Nature and frequency of preventive maintenance procedures N/A Problems experienced w ith control device w ithin the last five years; how

were problems solved? N/A Continuous monitoring method(s) used to monitor HVAF performance, including parameters monitored N/A Plans to replace or upgrade HVAF N/A**FORM C-7**

**AIR POLLUTION CONTROL**

**VII. Mist Eliminator**

For each mist eliminator: Mist Eliminator 1 Mist Eliminator 2 Mist Eliminator 3 Process line(s) (identification name/number) N/A Equipment/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan) N/A Latitude (decimal degrees, six decimal places) N/A Longitude (decimal degrees, six decimal places) N/A Stack or vent height (units) N/A Stack or vent diameter (units) N/A Manufacturer and model N/A Date of original installation N/A Type of mist eliminator N/A Gas flow rate to mist eliminator (acfm @ ° F) N/A Inlet gas temperature (° F) N/A Outlet gas temperature (° F) N/A Inlet grain loading (gr/dscf) N/A Outlet grain loading (gr/dscf) N/A Average stack opacity (%) N/A Velocity in mist eliminator (ft/sec) N/A Pressure drop (in. H 2 O gauge) N/A
For chevron blade mist eliminators: N/A Spacing between blades (in.) N/A W ashing frequency of blades N/A For mesh pad mist eliminators: N/A Number of pads or elements N/A Thickness of pad (in.) or element dimensions N/A Density of pad, (lb/ft3 ) N/A W ashing frequency of pad N/A Vendor guarantee on mist eliminator efficiency (attach copy) N/A Amount of wastewater generated (gpd) N/A Amount of wastewater recycled (gpd) N/A Amount of wastewater disposed of (gpd) N/A Method of wastewater disposal N/A Quantity of solid waste collected (lbs/yr) N/A Quantity of solid waste recycled (lbs/yr) N/A Quantity of solid waste disposed of (lbs/yr) N/A Method of solid waste disposal N/A Nature and frequency of preventive maintenance procedures N/A Problems experienced with control device within the last five years; how were problems solved? N/A Continuous monitoring method(s) used to monitor mist eliminator performance, including parameters monitored N/A Plans to replace or upgrade mist eliminator N/A

### FORM C-8

**AI R POLLUTION CONTROL** 

**VIII. Ventilation System**

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

### FORM C-9

**AI R POLLUTION CONTROL** 

**IX. Other**

For each other air pollution control devide (APCD): Other APCD 1 Other APCD 2 Other APCD 3 Process line(s) (identification name/number) 

### N/A Equipm ent/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan) 

### N/A Latitude (decimal degrees, six decimal places) 

### N/A Longitude (decimal degrees, six decimal places) 

### N/A Stack or vent height (units) 

### N/A Stack or vent diameter (units) 

### N/A Description 

### N/A**FORM D**

**PROCESS LINE STARTUP AND SHUTDOWN**

1. For each startup and shutdown (SS) that occurred during the past five years, please provide the following information requested in A. through J. All Startup and Shutdown for Cupolas are Controlled

A. Using the definitions provided above, indicate whether the event was a startup or shutdown; N/A (See Above Explanation) B. A description of the event, including identification of the emissions source or sources associated with the startup or shutdown; N/A (See Above Explanation) C. Whether any permit condition was exceeded and, if so, what permit condition was exceeded; N/A (See Above Explanation)

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 (See Above Explanation) E. The duration of the event; N/A (See Above Explanation) F. The actions taken to minimize emissions during the event, including the use of any backup control systems; N/A (See Above Explanation) 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 (See Above Explanation) 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 (See Above Explanation) 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 N/A (See Above Explanation) J. All monitoring data, including control system parameter monitoring, collected during each period of SS. N/A (See Above Explanation)

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 (See Above Explanation) 3. Please submit a copy of your SS plan if you are required to develop one. N/A (See Above Explanation) 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. N/A (See Above Explanation) 5. Please provide all monitoring data, including control system parameter monitoring, collected during periods of SS over the last 5 years. N/A (See Above Explanation) 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. N/A (See Above Explanation) Startup: the setting in operation of an affected source or portion of an affected source for any purpose. Shutdown: the cessation of operation of an affected source or portion of an affected source for any purpose.

### FORM E

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

Please provide any

existing emissions information and data covering hazardous air pollutants (HAP), particulate matter (PM), and carbon monoxide (CO) for each listed process. Identifythe appropriote box for which you are providing specific process inofrmation and/or pollutant emissions data.

Cupola Fiberization Fiber Collection Curing Cooling New em issions data for the purpose of completing the ICR request is being collected from Isolatek International as part of the North Am erican Insulation Manufacturers Association (NAIMA) through the "BTEC, Inc. Quality

Assurance Project Plan fo the Mineral W ool and Wo ol 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, carbony l sulfide, hydrogen flouride, metals (antimony

, arsenic, bery llium , cadmium, chromium, cobalt, lead, manganese, nickel, and selenium), mercury , and hexavalent chromium. {" **TBS** " - To be submitted from data collected at Isolatek International}

Cupola Fiberization Fiber Collection Curing Cooling Carbon monoxide (CO) **TBS** N/A N/A N/A N/A 

### Carbony l sulfide (COS) **TBS** N/A N/A N/A N/A 

### Particulate Matter (PM, PM2.5, PM10, PM condensable) **TBS** N/A N/A N/A N/A 

### Chromium compounds and Hexavalent Chromium (including anyCr speciation data) **TBS** N/A N/A N/A N/A 

### Other metal HAP (As, Be, Cd, Co, Hg, Pb, Mn, Sb, Se) **TBS** N/A N/A N/A N/A 

### Hydrogen Fluoride (HF) **TBS** N/A N/A N/A N/A 

### Hydrogen Chloride (HCl) **TBS** N/A N/A N/A N/A 

### Formaldehyde N/A N/A N/A N/A N/A 

### Phenol N/A N/A N/A N/A N/A 

### Methanol N/A N/A N/A N/A N/A 

### Other organic HAP N/A N/A N/A N/A N/A**FORM F-1**

**COST**

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

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

**II. Capital Costs** Base year

Total capital cost, including costs for individual pieces, if available. **III. A nnual Operating Costs**  Base year (most recent fiscal year) Total annual operating costs Maintenance materials and replacement parts (specify costs by item) Raw materials costs Labor ($/yr) for each labor class (hr/hr) for each labor class Utilities (breakdown for each utility) W aste treatment and/or disposal Costs associated with any work practices and pollution prevention techniques that are employed at your facility

Savings associated with heat recovery and wastewater and/or solid waste returned to process from APCD (or sold to another user) Indirect costs Other (specify)

Please provide the annual report to shareholders or equivalent for the most recent fiscal year. If reports are not available, provide annual sales and profits (or profit margin) for the most recent fiscal year. If company is publicly owned, please provide a web link to this information.

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

Can your product(s) be substituted by another product(s)? If so, please list your product(s) and substituted product(s). There are alternatives to mineral wool insulation, but these substitutes are notlikely to possess the same fire performance capabilities (mineral wool is nonflammable or non-combustible) as mineral wool, nor have recycled content (mineral wool can have up to 90% recycled content), nor possess many other attributes of mineral wool insulation products. Therefore, while substitutes exist, they lack the same performance characteristics that make mineral wool a unique insulation choice. Moreover, substitutes cannot be universally installed or applied in the traditional mineral wool applications. For Sections II - III (Except question on substitution) Isolatek International objects to this request because it seeks information that is not relevant to the EPA Administrator's review obligations pursuant to the Clean Air Section 112(d)(6) and 112(f)(2).

### FORM F-2

**COST**

**I. A ir Pollution Control Device (A**  **PCD)**

For each APCD: APCD 1 APCD 2 APCD 3 APCD ID Cupola Baghouse Process Unit ID

**II. Capital Costs** Base year APCD equipment purchase cost and w hat was included List the cost for each piece of auxiliary equipment for each APCD not included above Installation cost Land purchase cost Total capital cost Method of financing APCD Retrofit installation Field erected or modular

**III. A nnual Operating Costs**  Base year (most recent fiscal year)

Maintenance materials and replacement parts (specify costs by item) Raw materials costs Labor ($/y r) for each labor class (hr/hr) for each labor class Utilities (breakdow n for each utility ) W aste treatment and/or disposal Indirect costs Other (specify ) Total annual operating cost (most recent fiscal year)

Attach annual report to shareholders or equivalent for the most recent fiscal year For Sections II - III Isolatek International objects to this request because it seeks information that is not relevant to the EPA Administrator's review obligations pursuant to the Clean Air Section 112(d)(6) and 112(f)(2).