**FORM A -1** 

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

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

1. Legal Parent Company / Legal Corporate Name Industrial Insulation Group LLC 2. Address 2100 Line Dr 3. City Brunswick 4. State GA 5. Zip Code 6. County 7. Size of Company (approximate number of employees including all subsidiaries, branches, and related establishments owned): 425**FORM A -2** 

**FA CILITY INFORMA** 

**TION**

**II. Facility Information**

Facility Name IIG Minwool Facility Address Street 908 John Bussey Dr City Phenxi City State AL Zip Code 36869 County Russell Facility Coordinates Latitude (decimal degrees, six decimal places) 32.36179173 Longitude (decimal degrees, six decimal places) -91.57582171 Specific location represented (e.g., front door of main building, centroid of property , etc.) As listed in Title V documentation

Number of employees attached to the mineral wool production facility : CBI

Design capacity

of the plant (tons/y r) CBI

Ty pe(s) of process(es) (rotary spin, flame attenuation) at this plant Cupola, rotary spins, curing oven

Operation schedule hrs/day 24 days/y r approximately 244

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) Title V Alabama see attached permit

**III. Technical Contact** Original Contact: Name Jessie Pay ne Technical Contact Title Corporate EHS Manager Telephone 281-605-4630 or 334-507-9386-Cell Facsimile (Fax) 334-298-5429Email 

### paynej@iig-llc.com

**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? NA

Does the facility

manufacture other products in addition to mi neral wool? No

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

. NA

Are there any

HAP em issions associated with any co-located facilities? List unit operations, e.g., boiler, and pollutant/emissions NO**FORM A -2** 

**FA CILITY INFORMA** 

**TION**

**II. Facility Information**

Facility Name Facility Address Street City State Zip Code County Facility Coordinates Latitude (decimal degrees, six decimal places) Longitude (decimal degrees, six decimal places) Specific location represented (e.g., front door of main building, centroid of property , etc.)

Number of employees attached to the mineral wool production facility :

Design capacity

of the plant (tons/y r)

Ty pe(s) of process(es) (rotary spin, flame attenuation) at this plant

Operation schedule hrs/day days/y r

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)

**III. Technical Contact**

Name Technical Contact Title Telephone Facsimile (Fax) Interim Replacement: Rick Dolin Chief Product Analyst 970-858-9458 970-858-9641Email

**IV. Other**

Is the facility

a major source of HAP?

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?

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

.

Are there any

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

### dolinr@iig-llc.com**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 3 Process line identification name or numbers Board Pipe Ty pe of process line (e.g., Fiberization method) Fiberization Fiberrization Maximum annual production rate (tons/y r) Age of process line (y rs) 20 y r 20 y r

Remaining economic life of process line (y rs) Indefinite with ongoing

ma intenance program. Indefinite with ongoing

ma intenance program. List of products produced and most recent annual production (tons/y r; specify year) for each product Mineral W ool Mineral W ool

Please attach detailed schematics of each process line NA-**FORM B-2**

**PROCESS OPERA TIONS** 

**II. Raw Material Handling and Storage**

Cupola charge preparation Raw materials and proportions bywt (%) CBI Method(s) of convey ing each raw material to cupola Conveyor Binder and Additives List each raw material, including premixed materials, in the binder formulation and its proportion bywt (%) CBI List steps in preparing binder, including storage temperature ( ° F) and holding time (hrs) CBI Total y early

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

year) CBI Are binder storage and mixing tanks vented to outside/inside? Inside

Method of treating vent air from storage and mix tanks None Emission control during liquid raw material transfer from vehicles to storage tanks. Closed system Describe future source reduction plans and schedules to reformulate binders; List each constituent, proportions wt (%), cost ($/gal) for reformulation None at this time**FORM B-3**

**PROCESS OPERA TIONS** 

**III. Cupola/furnace**

For each cupola: Cupola 1 Cupola 2 Cupola 3 Process unit identification name/number 1 Process line(s) served (identification name/number) 2 Latitude (decimal degrees, six decimal places) 32.430118 Longitude (decimal degrees, six decimal places) -84.978139 Stack or vent height (units) Stack 200 ft Stack or vent diameter (units) Stack 8 ft Dia. Manufacturer and model Jungers Verstad AB Date of original installation 1988-1989 Estimate of remaining lifetime (y rs) Major rebuilds: W hat constitutes a major rebuild Frequency

of a major rebuild NA Cost of ty pical major rebuild NA Date of last major rebuild NA Purpose of last major rebuild NA Increase or decrease in emissions NA Fuel ty pe: coke, electric, gas, or oil NA Mod or change of ops that affects permiting requirements Continued maintenance can maintain indefinite life,

Fuel consumption rate (KW /ton of melt or Btu/ton of melt) NA Design production rate (tons/day ) NA Actual glass pull rate (tons/day ) NA Exhaust air flow rate (acfm @ ° F) NA Temperature ( ° F) of melt as it exits the cupola NA

Is oxygen enrichment used to supplement combustion air NA Quantity

of oxygen supplied for enrichment (cu. Ft. O2/ton coke) NA Nature and frequency of routine/preventive maintenance procedures NA Describe process modification(s) since 1999 that reduce emissions None Describe future source reduction plans and schedules**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 Process line(s) served (identification name/number) Board/Pipe Latitude (decimal degrees, six decimal places) 32.430149 Longitude (decimal degrees, six decimal places) -84.978027 Stack or vent height (units) Stack 200 feet Stack or vent diameter (units) Stack Dia 8.5 feet Number of fiber forming devices (spinners) per line 2 Method of attenuation fiber (air, centrifical force, or both) Both Major rebuilds:

Wh at constitutes a major rebuild Frequency

of a major rebuild NA Cost of ty pical major rebuild NA Date of last major rebuild NA Purpose of last major rebuild NA Increase or decrease in emissions NA If forming section is modular, i.e., more than one forming and collection area per line, indicate the number of modules and air plenum s. NA Presence of water overspray and application range (gpm) NA Binder applied and application rate (gpm) CBI Other material applied (annealing oil or oil/water emulsion) and application rate (gpm) CBI Temperature of binder when applied to the fibers ( ° F) CBI Forming air flow rate (acfm @ °F) CBI

Percent of forming air recirculated and percent exhausted CBI Nature and frequency of routine/preventive maintenance procedures Based on SSM/OMM Plan attached. Describe process modification(s) since 1999 that reduce

em issions None Describe future source reduction plans and schedules Mod or change of ops that affects permiting requirementsFiberization m ethod (e.g., Downey process or Youger/Powell process) Number of rotors Configuration of rotor(s) Amount of material that remains non-fiberized shot Exhaust air flow rate (acfm @ ° F)**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 1 Process line(s) served (identification name/number) Board/Pipe Latitude (decimal degrees, six decimal places) 32.430149 Longitude (decimal degrees, six decimal places) -84.97812 Stack or vent height (units) Stack 200 feet Stack or vent diameter (units) Stack Dia 8.5 feet Method of fiber collection from fiberization Rotating Drum Manufacturer and model of collection chamber Date of original installation Major rebuilds: W hat constitutes a major rebuild Frequency

of a major rebuild NA Cost of ty pical major rebuild NA Date of last major rebuild NA Purpose of last major rebuild NA Increase or decrease in emissions NA

Air flow rate (acfm @ ° F) in pneumatic fiber convey ing CBI Exhaust air flow rate (acfm @ °F) Residence time of product (mins) (time spent in collection device) CBI

Method of evenly

distributing fibers onto conveyor belt Formed mat thickness (in.) Varies Nature and frequency of routine/preventive

ma intenance procedures Monthly /Annually

PM Describe process modification(s) since 1999 that reduce emissions None

Describe future source reduction plans and schedules Mod or change of ops that affects permiting requirements**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 1 Process line(s) served (identification name/number) Board/Pipe Latitude (decimal degrees, six decimal places) 32.430246 Longitude (decimal degrees, six decimal places) -84.97802 Stack or vent height (units) Stack 200 feet Stack or vent diameter (units) Stack Dia 8.5 feet Method of curing Gas Heat Manufacturer and model Jungers Verstad AB Date of original installation Major rebuilds: W hat constitutes a major rebuild Frequency

of a major rebuild NA Cost of ty pical major rebuild NA Date of last major rebuild NA Purpose of last major rebuild NA Increase or decrease in emissions NA Fuel ty pe: electric, gas, or oil Gas Heat Fuel consumption rate (KW /hr or BTU/hr) Curing temperature ( ° F) 354 Moisture content wt (%) of formed mat: inlet 4.8 outlet 4.8 Exhaust air flow rate (acfm @ ° F) from curing Residence time of product (mins) Variable Binder content of cured product (LOI) Nature and frequency of routine/preventive maintenance procedures See attached OMM/SSM Describe process modification(s) since 1999 that reduce

em issions None Describe future source reduction plans and schedules None Mod or change of ops that affects permiting requirements**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 

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

### Board Latitude (decimal degrees, six decimal places) 32.430753 Longitude (decimal degrees, six decimal places) -84.978309 Stack or vent height (units) NA Stack or vent diameter (units) NA Cooling air flow rate (acfm @ ° F) 

### NA Percentage of cooling air recirculated (if any ) 

### NONE Cooling air temperature (°F) 

### NA Exhaust air flow rate (acfm @ °F) 

### NA Nature and frequency of routine/preventive maintenance procedures 

### Monthly/Annually Describe process modification(s) since 1999 that reduce

em issions 

### NONE Describe future source reduction plans and schedules**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 HAPs you identified in Form E. You m ust specify

the year in which the facility im plem ented the practice/technique and identify the emission reductions (if measured) from these practices/techniques. NONE**FORM C-1**

**AI R POLLUTION CONTROL** 

**I. Electrostatic Precipitator (ESP)** (none)

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

of solid waste collected (lbs/y r) Quantity

of solid waste recycled (lbs/y r) Quantity

of solid waste disposed of (lbs/y r)Method of solid waste disposal

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

plans to replace or upgrade ESP**FORM C-2**

**AI R POLLUTION CONTROL** 

**II. Scrubber** (none)

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

Source of scrubbing water and ty pe of pretreatment. Substance(s) added as part of pretreatment and amount used (gpm or lbs/hr) HAP composition of wastewater (mg/L) Concentration (mg/L) of dissolved and suspended solids in scrubbing water Scrubbing water temperature ( ° F) Liquid/gas ratio (gal/10 3 acfm) Pressure drop across scrubber (in. H 2 O gauge) Amount of wastewater generated (gpd) Amount of wastewater recy cled (gpd) Amount of wastewater disposed of (gpd)Method of wastewater disposal

Quantity

of solid waste collected (lbs/y r) Quantity

of solid waste recycled (lbs/y r) Quantity

of solid waste disposed of (lbs/y r) Method of solid waste disposal Vendor guarantee on scrubber efficiency (attach copy ) Nature and frequency of preventive maintenance procedures Problems experienced with control device within the last five years; how were problem s solved? Continuous monitoring method(s) used to monitor scrubber performance, including parameters monitored Plans to replace or upgrade scrubber**FORM C-3**

**AI R POLLUTION CONTROL** 

**III. Mechanical Collector** (none)

For each mechanical collector: Mechanical Collector 1 Mechanical Collector 2 Mechanical Collector 3 Process line(s) (identification name/number) Equipm ent/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan) Latitude (decimal degrees, six decimal places) Longitude (decimal degrees, six decimal places) Stack or vent height (units) Stack or vent diameter (units) Manufacturer and model Date of original installation Ty pe of mechanical collector Gas flow rate to collector (acfm @ ° F) Inlet gas temperature ( ° F) Outlet gas temperature ( ° F) Inlet grain loading (gr/dscf) Outlet grain loading (gr/dscf) Average stack opacity (%) Overall pressure drop (in. H 2 O gauge) Vendor guarantee on mechanical collector efficiency (attach copy ) Quantity

of solid waste collected (lbs/y r) Quantity

of solid waste recycled (lbs/y r) Quantity

of solid waste disposed of (lbs/y r) Method of solid waste disposal

Nature and frequency of preventive maintenance procedures Problems experienced with control device within the last five ye ars; how were problems solved? Continuous monitoring method(s) used to monitor performance, including parameters monitored Plans to replace or upgrade mechanical collector**FORM C-4**

**AI R POLLUTION CONTROL** 

**IV. Fabric Filter**

For each fabric filter: Fabric Filter 1 Fabric Filter 2 Fabric Filter 3 Process line(s) (identification name/number) 

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

### Curing Oven Latitude (decimal degrees, six decimal places) Longitude (decimal degrees, six decimal places) Stack or vent height (units) 200 ft

Manufacturer and model 

### Custom Built Date of original installation 

### 1989 Number of compartments Number of bags per compartment 

### 315

Filter material and coatings applied 

### See attached Filtration Fabric Datasheet Fabric weight (oz/yd 2 ) 

### 14 Filter surface area (ft 2 ) 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 (%) 

### <1 Overall pressure drop (in. H 2 O gauge) Method and frequency of bag cleaning Vendor guarantee on fabric filter efficiency (attach copy ) Quantity

of solid waste collected (lbs/y r) Quantity

of solid waste recycled (lbs/y r) Quantity

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

### See OMM/SSM 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 

### Pressure/Temp Plans to replace or upgrade fabric filter 

### No**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) 

### Envirotech NONE NONE

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

### Controls Cupola, Fiber collection, emission point stack # 1. NONE NONE Latitude (decimal degrees, six decimal places) 32.42989 

### NONE NONE Longitude (decimal degrees, six decimal places) -84.978132 

### NONE NONE Stack or vent height (units) 200 

### NONE NONE Stack or vent diameter (units) 8.5 feet 

### NONE NONE Manufacturer and model 

### Envirotech NONE NONE Date of original installation 

### 1989 NONE NONE Fuel ty pe: gas or oil 

### Natural Gas NONE NONE Fuel consumption rate (BTU/hr) 

### NONE NONE Inlet gas flow rate (acfm @ ° F) 

### 7080 NONE NONE Inlet gas temperature ( ° F) 

### 376 NONE NONE Combustion chamber gas temperature ( ° F) 

### 1500 NONE NONE Outlet gas temperature ( ° F) 

### 586 NONE NONE Inlet grain loading (gr/dscf) 

### NONE NONE Outlet grain loading (gr/dscf) 

### NONE NONE Average stack opacity (%) 

### Less than 1% NONE NONE Excess air (%) 

### NONE NONE Residence time (sec) at temperature ( ° F) 

### 1 sec @ 1500 NONE NONE Percent heat recovery 

### NONE NONE Vendor guarantee on incinerator efficiency (attach copy ) 

### Unavailable NONE NONE

Nature and frequency of preventive maintenance procedures 

### See attached MACT/SSM NONE NONE Problems experienced with control device within the last five ye ars; how were problems solved? 

### NONE NONE NONE Continuous monitoring method(s) used to monitor incinerator performance, including parameters monitored 

### NONE NONEPlans to replace or upgrade thermal incinerator 

### None NONE NONE**FORM C-6**

**AI R POLLUTION CONTROL** 

**VI. High Velocity A ir Filter (HVA**  **F)** (none)

For each HVAF: HVAF 1 HVAF 2 HVAF 3 Process line(s) (identification name/number) Equipm ent/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan) Latitude (decimal degrees, six decimal places) Longitude (decimal degrees, six decimal places) Stack or vent height (units) Stack or vent diameter (units) Manufacturer and model Date of original installation Inlet gas flow rate (acfm @ ° F) Inlet gas temperature ( ° F) Outlet gas temperature ( ° F) Inlet grain loading (gr/dscf) Outlet grain loading (gr/dscf) Average stack opacity (%)
W ater spray

pressure (psig), if applicable
W ater spray

rate (gpm), if applicable Filter face velocity

(acfm/ft 2 ) Maximum pressure drop across mat (in. H 2 O gauge) Vendor guarantee on HVAF efficiency (attach copy ) Method and frequency of filter mad advancement Amount of wastewater generated (gpd) Amount of wastewater recy cled (gpd) Amount of wastewater disposed of (gpd) Method of wastewater disposal Quantity

of solid waste collected (lbs/y r) Quantity

of solid waste recycled (lbs/y r) Quantity

of solid waste disposed of (lbs/y r) Method of solid waste disposalNature and frequency of preventive maintenance procedures Problems experienced with control device within the last five years; how were problems solved? Continuous monitoring method(s) used to monitor HVAF performance, including parameters monitored Plans to replace or upgrade HVAF**FORM C-7**

**AI R POLLUTION CONTROL** 

**VII. Mist Eliminator** (none)

For each mist eliminator: Mist Eliminator 1 Mist Eliminator 2 Mist Eliminator 3 Process line(s) (identification name/number) Equipm ent/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan) Latitude (decimal degrees, six decimal places) Longitude (decimal degrees, six decimal places) Stack or vent height (units) Stack or vent diameter (units) Manufacturer and model Date of original installation Ty pe of mist eliminator Gas flow rate to mist eliminator (acfm @ ° F) Inlet gas temperature ( ° F) Outlet gas temperature ( ° F) Inlet grain loading (gr/dscf) Outlet grain loading (gr/dscf) Average stack opacity (%) Velocity

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

of pad, (lb/ft 3 )
W ashing frequency of pad Vendor guarantee on mist eliminator efficiency (attach copy ) Amount of wastewater generated (gpd) Amount of wastewater recy cled (gpd)Amount of wastewater disposed of (gpd)

Method of wastewater disposal Quantity

of solid waste collected (lbs/y r) Quantity

of solid waste recycled (lbs/y r) Quantity

of solid waste disposed of (lbs/y r) Method of solid waste disposal Nature and frequency of preventive maintenance procedures Problems experienced with control device within the last five ye ars; how were problems solved? Continuous monitoring method(s) used to monitor mist eliminator performance, including parameters monitored Plans to replace or upgrade mist eliminator**FORM C-8**

**AI R POLLUTION CONTROL** 

**VIII. Ventilation System** (none)

For each ventilation system: Ventilation System 1 Ventilation System 2 Ventilation System 3 Process line(s) (identification name/number) Equipm ent/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan) Latitude (decimal degrees, six decimal places) Longitude (decimal degrees, six decimal places) Stack or vent height (units) Stack or vent diameter (units) For general or building ventilation: Ventilation system used Airflow control system used Number of air changes per hour For unit or local ventilation: Enclosure or hood design used Volume of enclosure or hood Capture velocity (ft/sec) Distance between hood and emission source (ft)**FORM C-9**

**AI R POLLUTION CONTROL** 

**IX. Other** (none)

For each other air pollution control devide (APCD): Other APCD 1 Other APCD 2 Other APCD 3 Process line(s) (identification name/number) Equipm ent/process(es) controlled. Include emission point designations (e.g., E3, E4 from plot plan) Latitude (decimal degrees, six decimal places) Longitude (decimal degrees, six decimal places) Stack or vent height (units) Stack or vent diameter (units) Description**FORM D**

**PROCESS LINE STA RTUP A**  **ND 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.

A. Using the definitions provided above, indicate whether the event was a startup or shutdown; None B. A description of the event, including identification of the

em issions source or sources associated with the startup or shutdown; None C. W hether any

permit condition was exceeded and, if so, what permit condition was exceeded; None

D. W hether the event was covered by any contingency

plan for controlling emissions during startup and shutdown events and, if so, whether the plan was followed; if the plan was not followed, why not; None E. The duration of the event; NA F. The actions taken to minimize emissions during the event, including the use of any backup control systems; None 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 ; None H. W hether the emission profile of each unit was different during startup and shutdown than during normal operating conditions and, if so, how emissions were different and why ; please provide any supporting information; NA 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 NA J. All monitoring data, including control system parameter

mo nitoring, collected during each period of SS. NA 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.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

ty pes of startup or shutdown events that you have been able to elim inate? If so, please describe the ty pe of event and explain how these events were elim inated. None 3. Please submit a copy of your SS plan if you are required to develop one. Attached 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. Attached 5. Please provide all m onitoring data, including control system parameter monitoring, collected during periods of SS over the last 5 ye ars. Attached 6. Optional: Do you wish to recommend a standard that would apply during startup or shutdown? If so, please describe the event to which the standard would apply ; the recommended standard (this could be an emission limitation, work practice, or operational standard) that would apply during the period; the basis for the recommended standard; why and how the standard would m inim ize

em issions during the event; and how would compliance be determined and/or monitored. None**FORM E**

**PRESENCE OF A IR POLLUTA**  **NTS IN EMISSION POINTS** (testing reported separately )

Please provide any

existing emissions information and data covering hazardous air pollutants (HAP), particulate matter (PM), and carbon monoxide (CO) for each listed process. Identify the appropriote box for which you are providing specific process inofrmation and/or pollutant emissions data. Cupola Fiberization Fiber Collection Curing Cooling Carbon monoxide (CO) Carbony l sulfide (COS) Particulate Matter (PM, PM2.5, PM10, PM condensable) Chromium compounds and Hexavalent Chromium (including any Cr speciation data) Other metal HAP (As, Be, Cd, Co, Hg, Pb, Mn, Sb, Se) Hydrogen Fluoride (HF) Hydrogen Chloride (HCl) Formaldehy de Phenol Methanol Other organic HAP**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 Process Line ID

**II. Capital Costs** Base y ear

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

Savings associated with heat recoveryand 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 y ear. If reports are not available, provide annual sales and profits (or profit margin) for the most recent fiscal ye ar. If company

is publicly

owned, please provide a web link to this information.

Identify the market range (regional, national, international) of y our products.Can your product(s) be substituted byanother product(s)? If so,

please list y our product(s) and substituted product(s).**FORM F-2**

**COST**

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

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

**II. Capital Costs** Base y ear APCD equipment purchase cost and what was included List the cost for each piece of auxiliaryequipment 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 y ear (most recent fiscal y ear)

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

Attach annual report to shareholders or equivalent for the most recent fiscal y ear