FORM A-1PARENT COMPANY INFORMATIONI. Parent Company / Legal Corporate Owner Information1. Legal Parent Company / Legal Corporate NameOwens Corning Insulating Systems, LLC2. AddressOne Owens Corning Parkway3. CityToledo4. StateOhio5. Zip Code436596. CountyLucas7. Size of Company (approximate number of employees includingall subsidiaries, branches, and related establishments owned):16,280FORM A-2FACILITY INFORMATIONII. Facility InformationFacility NameOwens Corning Insulating Systems, LLCStreet4340 West 850 SouthCitySalt Lake CityStateUtahZip Code84104CountySalt LakeLatitude (decimal degrees, six decimal places)40.750475Longitude (decimal degrees, six decimal places)111.995214Specific location represented (e.g., front door of main building, centroidof property, etc.)Centroid of PropertyNumber of employees attached to the wool fiberglass manufacturingfacility:21Design capacity of the plant (tons/yr)Type(s) of process(es) (rotary spin, flame attenuation) at this plantRotary Spinhrs/day24days/yr365Identify what state and local air pollution rulesand regulations, includingpermit requirements, your plant is subject to. (Please provide copies ofpermit(s) and permit IDs)Applicable requirements referenced in State Operating PermitAN0033007-04. Provided on CD.NameMike PettisTechnical Contact TitleISB Environmental LeaderTelephone740-877-7087Facsimile (Fax)740-328-2696EmailMike.Pettis@owenscorning.comFacility AddressFacility CoordinatesOperation scheduleIII. Technical ContactFORM A-2FACILITY INFORMATIONIs the facility a major source of HAP?NoIf No, did the facility take a limit of its potential HAP emissions to avoidclassification as a major source:NoDoes the facility manufacture other productsin addition to woolfiberglass?NoIf Yes, list the other products manufacturedat the facility.N/AAre there any HAP emissions associated with any co-located facilities?List unit operations, e.g., boiler, and pollutant/emissions.N/AIV. OtherFORM B-1PLANT OPERATIONSI. Overview of Plant OperationsNumber of process lines. Include lines that are currentlyoperational or that are temporarily shutdown. (Donotinclude lines permanently shutdown).2For each process line:Process Line 1Process Line 2Process line identification names or numbersBonded LineUnbonded LoosefillType of process line (e.g., rotary spin, flame attenuation) Rotary Spin Rotary SpinMaximum annual production rate (tons/yr)Age of process equipment (yrs) Not known. Acquiredfacility in 1995.Not known. Acquiredfacility in 1995.Remaining economic life of process line (yrs) N/A.Continuedmaintenance canmaintain indefinite life.N/A. Continuedmaintenance canmaintain indefinite life.List of products produced and most recent annualproduction (tons/yr; specify year) for each productPlease attach detailed schematics of each process line. Provided on CD. Provided on CD.FORM B-2PLANT OPERATIONSII. Process - Raw materials Handling and StorageMolten glass preparationRaw materials and proportions by wt (%) Industry information provided for representativeness:Soda Ash (9%), Borax (12%), Cullet (34%), Limestone(9%), Sand (31%).Method(s) of conveying each raw material to furnace/pots Pneumatic conveying system transports batch rawmaterials from delivery trucks to storage silos. The rawmaterials are weighed and mixed. The batch ispneumatically transferred to furnace bins and thento thefurnaces.Binder and AdditivesList each raw material, including premixed materials, in the binderformulation and its proportion by wt (%)List steps in preparing binder, including storage temperature (°F)and holding time (hrs)Bonded Line: The above listed binder ingredients aremetered into binder mix tanks. Mixed binder is transferredto a recirculating tank. All storage temperaturesareambient. Total holding time is approximately 45 minutes.Unbonded Loose Fill Line: N/A - Unbonded loose fillis notmanufactured with binder.Total yearly consumption of binder (gal/yr)Cost of binder ($/gal) for most recent year (specify year)N/A. Did not use binder in 2009.Are binder storage and mixing tanks vented tooutside/inside? Binder mix and storage tanks are vented inside.Method of treating vent air from storage andmix tanksN/AEmission control during liquid raw material transfer from vehiclesto storage tanks.N/ADescribe future source reduction plans and schedules toreformulate binders; List each constituent, proportions wt (%), cost($/gal) for reformulationThe Company has established goals to reduce theenvironmental footprint of our manufacturing operationsas part of our sustainability efforts. These goalsarefocused on reducing waste-to-landfill, GHG, waterconsumption, VOC’s, particulate matter, NOx and energy.FORM B-3PLANT OPERATIONSIII. Process - Glass Melting FurnaceFor each Glass Melting Furnace:Furnace 1Furnace 2Process unit identification name/number#1 (North)#2 (South)Process line(s) served (identification name/number) SL1 (Bonded) and U2(Unbonded Loose Fill)SL1 (Bonded) and U2(Unbonded Loose Fill)Latitude (decimal degrees, six decimal places)40.751501740.7514936Longitude (decimal degrees, six decimal places)-111.9958811-111.9958811Stack or vent height (units)76.59 ft.76.59 ft.Stack or vent diameter (units)1 ft.1 ft.Manufacturer and model Not known (spot melter).Acquired facility in 1995.Not known (spot melter).Acquired facility in 1995.Date of original installationNot known. Acquired facility in1995.Not known. Acquired facility in1995.Estimate of remaining lifetime (yrs) N/A. Continued maintenancecan maintain indefinite life.N/A. Continued maintenancecan maintain indefinite life.Major rebuilds:What constitutes a major rebuildFrequency of a major rebuildN/AN/ACost of typical major rebuildN/AN/ADate of last major rebuildN/AN/APurpose of last major rebuildN/AN/AIncrease or decrease in emissionsN/AN/AFuel type: electric, gas, or oilElectricElectricFuel consumption rate (KW/ton of glass or Btu/ton ofglass)List HAPs that are in refractory materialChromium CompoundsChromium CompoundsFORM B-3PLANT OPERATIONSIII. Process - Glass Melting FurnaceFor each Glass Melting Furnace:Furnace 1Furnace 2Process unit identification name/number#1 (North)#2 (South)Process line(s) served (identification name/number) SL1 (Bonded) and U2(Unbonded Loose Fill)SL1 (Bonded) and U2(Unbonded Loose Fill)Design production rate (tons/day)Actual glass pull rate (tons/day)Vent gas flow rate (acfm @°F)Temperature (°F) of molten glass in furnace andforehearth (if applicable)Nature and frequency of routine/preventive maintenanceproceduresGeneral maintenance activitiesfollow a prescribed schedulethat is detailed in themaintenance tracking system.Refractory repairs arecompleted infrequently andonly as necessary.General maintenance activitiesfollow a prescribed schedulethat is detailed in themaintenance tracking system.Refractory repairs arecompleted infrequently andonly as necessary.Describe process modification(s) since 1999 that reduceemissionsThe Company has establishedgoals to reduce theenvironmental footprint of ourmanufacturing operations aspart of our sustainabilityefforts. These goals arefocused on reducing waste-tolandfill, GHG, waterconsumption, VOC's,particulate matter, NOx andenergy.The Company has establishedgoals to reduce theenvironmental footprint of ourmanufacturing operations aspart of our sustainabilityefforts. These goals arefocused on reducing waste-tolandfill, GHG, waterconsumption, VOC's,particulate matter, NOx andenergy.Describe future source reduction plans and schedules None currently approved orscheduled at this time.None currently approved orscheduled at this time.FORM B-4PLANT OPERATIONSIV. Process - Forming -- Rotary Spin / Flame AttenuationFor each Forming Operation -- Rotary Spin/Flame AttenuationForming Operation 1Forming Operation 2Process unit identification name/number SL1 Forming N/A - Unbonded Loose Fill- lineis not rotary spine/flameattenuation.Process line(s) served (identification name/number)SL1 (Bonded)N/ALatitude (decimal degrees, six decimal places)40.7515131N/ALongitude (decimal degrees, six decimal places)-111.9959186N/AStack or vent height (units)81.28 ftN/AStack or vent diameter (units)4.5 ft.N/ANumber of fiber forming devices (spinners) per line.N/AMethod of attenuating fiber (e.g., air, flame, or air and flame).Indicate type of burner used (if flame).Air and Flame N/AIs there a forehearth between the furnace andthe formingsection?Yes N/AMajor rebuilds:What constitutes a major rebuild The company undertakesroutine repair and replacementprojects. As with the furnace,these projects are normally “asis” maintenance projects that donot impact the formingemissions. Therefore, thecompany does not considerthese to be major rebuilds forthe purpose of this ICR.N/AFrequency of a major rebuildN/AN/ACost of typical major rebuildN/AN/ADate of last major rebuildN/AN/APurpose of last major rebuildN/AN/AIncrease or decrease in emissionsN/AN/AIf modular, number of modules and plenumsN/APresence of water overspray and application rate (gpm)N/ABinder applied and application rate (gpm)N/AOther material applied and application rate (gpm)N/AN/AFORM B-4PLANT OPERATIONSIV. Process - Forming -- Rotary Spin / Flame AttenuationFor each Forming Operation -- Rotary Spin/Flame AttenuationForming Operation 1Forming Operation 2Process unit identification name/number SL1 Forming N/A - Unbonded Loose Fill- lineis not rotary spine/flameattenuation.Process line(s) served (identification name/number)SL1 (Bonded)N/ATemperature of glass fiber when binder is applied (°F)N/ATemperature of binder when applied to fibers(°F)N/AMethod of evenly distributing fibers onto forming conveyor Compressed air lapping system N/AFormed mat thickness (in.)1" - 6" as formed, up to 15" onramp.N/AForming air flow rate (acfm @ °F)N/APercent of forming air recirculated and percent exhausted None recirculated, 100%exhausted.N/ANature and frequency of routine/preventive maintenanceproceduresGeneral maintenance activitiesfollow a prescribed schedulethat is detailed in themaintenance tracking system.Repairs and replacements areperformed when required duringunscheduled downtimes.Basic, routine cleaning occursevery 6 to 12 weeks.Significant repairs such aschain and sprocketreplacement, frame repair andtrack replacement generallyoccur with refractoryreplacement of the furnace.N/AFORM B-4PLANT OPERATIONSIV. Process - Forming -- Rotary Spin / Flame AttenuationFor each Forming Operation -- Rotary Spin/Flame AttenuationForming Operation 1Forming Operation 2Process unit identification name/number SL1 Forming N/A - Unbonded Loose Fill- lineis not rotary spine/flameattenuation.Process line(s) served (identification name/number)SL1 (Bonded)N/ADescribe process modification(s) since 1999 that reduceemissionsThe Company has establishedgoals to reduce theenvironmental footprint of ourmanufacturing operations aspart of our sustainability efforts.These goals are focused onreducing waste-to-landfill, GHG,water consumption, VOC's,particulate matter, NOx andenergy.N/ADescribe future source reduction plans and schedules None currently approved orscheduled at this time.N/AFORM B-5PLANT OPERATIONSV. Process - CuringFor eachCuring Oven:Curing Oven 1Curing Oven 2Process unit identification name/number SL1 Curing N/A - Unbonded Loose Fill- linedoes not have curing.Process line(s) served (identification name/number) SL1 (Bonded) N/ALatitude (decimal degrees, six decimal places)40.7515131N/ALongitude (decimal degrees, six decimal places)-111.9959186N/AStack or vent height (units)81.28 ftN/AStack or vent diameter (units)4.5 ft.N/AMethod of curingN/AManufacturer and model Not known. Acquired facility in1995.N/ADate of original installation Not known. Acquired facility in1995.N/AMajor rebuilds:What constitutes a major rebuild The company undertakesroutine repair and replacementprojects. As with the furnace,these projects are normally “asis” maintenance projects that donot impact the oven emissions.Therefore, the company doesnot consider these to be majorrebuilds for the purpose of thisICR.N/AFrequency of a major rebuildN/AN/ACost of typical major rebuildN/AN/ADate of last major rebuildN/AN/APurpose of last major rebuildN/AN/AIncrease or decrease in emissionsN/AN/AFuel type: electric, gas, or oilNatural GasN/AFuel consumption rate (KW/hr or BTU/hr)N/AMoisture content wt (%) of formed mat:inlet2 - 4%N/AFORM B-5PLANT OPERATIONSV. Process - CuringFor eachCuring Oven:Curing Oven 1Curing Oven 2Process unit identification name/number SL1 Curing N/A - Unbonded Loose Fill- linedoes not have curing.Process line(s) served (identification name/number) SL1 (Bonded) N/Aoutlet<0.5%N/AAir flow rate (acfm @°F) from curing61,377 acfm @ 105 °F(combined air flow from formingand oven)N/AExhaust air temperature (°F)105 °FN/AResidence time of product (mins)N/ABinder content of cured product (LOI)N/ANature and frequency of routine/preventivemaintenance proceduresGeneral maintenance activitiesfollow a prescribed schedulethat is detailed in themaintenance tracking system.Repairs and replacements areperformed when required duringunscheduled downtimes.Basic, routine cleaning occursevery 6 to 12 weeks.Significant repairs such aschain and sprocketreplacement, frame repair andtrack replacement generallyoccur with refractoryreplacement of the furnace.N/AFORM B-5PLANT OPERATIONSV. Process - CuringFor eachCuring Oven:Curing Oven 1Curing Oven 2Process unit identification name/number SL1 Curing N/A - Unbonded Loose Fill- linedoes not have curing.Process line(s) served (identification name/number) SL1 (Bonded) N/ADescribe process modification(s) since 1999 thatreduce emissionsThe Company has establishedgoals to reduce theenvironmental footprint of ourmanufacturing operations aspart of our sustainability efforts.These goals are focused onreducing waste-to-landfill, GHG,water consumption, VOC's,particulate matter, NOx andenergy.N/ADescribe future source reduction plans andschedulesNone currently approved orscheduled at this time.N/AFORM B-6PLANT OPERATIONSVI. Process - CoolingFor eachCooling Operation: Cooling Operation 1 Cooling Operation 2Process unit identification name/number SL1 Cooling N/A - Unbonded Loose Fill -Line does not have cooling.Process line(s) served (identification name/number) SL1 (Bonded) N/ALatitude (decimal degrees, six decimal places)40.7516769N/ALongitude (decimal degrees, six decimal places)-111.9952217N/AStack or vent height (units)46.93 ft.N/AStack or vent diameter (units)1.83 ft.N/ACooling air flow rate (acfm @°F)5,236 acfm @ 78 °F N/APercentage of cooling air recirculated (if any) None N/ACooling air temperature (°F) 78 °F N/ANature and frequency of routine/preventivemaintenance proceduresGeneral maintenance activitiesfollow a prescribed schedulethat is detailed in themaintenance tracking system.Repairs and replacements areperformed when requiredduring unscheduleddowntimes. Basic, routinecleaning occurs every 6 to 12weeks. Significant repairssuch as chain and sprocketreplacement, frame repair andtrack replacement generallyoccur with refractoryreplacement of the furnace.N/AFORM B-6PLANT OPERATIONSVI. Process - CoolingFor eachCooling Operation: Cooling Operation 1 Cooling Operation 2Process unit identification name/number SL1 Cooling N/A - Unbonded Loose Fill -Line does not have cooling.Process line(s) served (identification name/number) SL1 (Bonded) N/ADescribe process modification(s) since 1999 thatreduce emissionsThe Company has establishedgoals to reduce theenvironmental footprint of ourmanufacturing operations aspart of our sustainabilityefforts. These goals arefocused on reducing waste-tolandfill, GHG, waterconsumption, VOC's,particulate matter, NOx andenergy.N/ADescribe future source reduction plans and schedules None currently approved orscheduled at this time.N/AFORM B-7PLANT OPERATIONSVII. Process - Use of SolventsUse of SolventsVolatile solvents used at your facility (where and how used) N/A. No HAP-containing solvents usedin themanufacturing process.List each solvent used and quantity (gal/yr) N/A. No HAP-containing solvents used in themanufacturing process.Emission control device(s) used to control emissions from solventusage/storage?N/A. No HAP-containing solvents used in themanufacturing process.FORM B-8PROCESS OPERATIONSVIII. Pollution PreventionPlease describe any work practices, pollution prevention techniques,and control strategies evaluated and/or implementedat each processunit 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 thepractice/technique and identify the emission reductions (if measured)from these practices/techniques.The Company has established goals to reduce theenvironmental footprint of our manufacturing operationsas part of our sustainability efforts. These goalsarefocused on reducing waste-to-landfill, GHG, waterconsumption, VOC's, particulate matter, NOx and energy.FORM C-1AIR POLLUTION CONTROLI. Electrostatic Precipitator (ESP)Not applicable to this facility.For each ESP:ESPProcess line(s) (identification name/number)N/AEquipment/process(es) controlled. Include emission pointdesignations (e.g., E3, E4 from plot plan)N/ALatitude (decimal degrees, six decimal places)N/ALongitude (decimal degrees, six decimal places)N/AStack or vent height (units)N/AStack or vent diameter (units)N/AManufacturer and modelN/ADate of original installationN/ANumber of collection plates and configurationN/AGas flow rate to ESP (acfm @°F)N/AInlet gas temperature (°F)N/AOutlet gas temperature (°F)N/AInlet grain loading (gr/dscf)N/AOutlet grain loading (gr/dscf)N/AAverage stack opacity (%)N/APressure drop across ESP (in. H2O gauge) N/APlate area (ft2)N/AVendor guarantee on ESP efficiency (attach copy)N/AMethod of plate cleaning and frequencyN/AFlow rate of plate wash water to ESP (gpm), if applicableN/ATemperature of plate wash water to ESP (°F), if applicableN/ASource of plate wash water used for cleaning,if applicableN/AConcentration (mg/l) of dissolved and suspended solids in platewash water, if applicableN/AConditioning agents used and amounts (in gpmor lbs/hr), ifapplicableN/AAmount of wastewater generated (gpd), if applicableN/AAmount of wastewater recycled (gpd), if applicableN/AAmount of wastewater disposed of (gpd), if applicableN/AMethod of wastewater disposal, if applicableN/AQuantity of solid waste collected (lbs/yr)N/AQuantity of solid waste recycled (lbs/yr)N/AQuantity of solid waste disposed of (lbs/yr)N/AFORM C-1AIR POLLUTION CONTROLI. Electrostatic Precipitator (ESP)Not applicable to this facility.For each ESP:ESPProcess line(s) (identification name/number)N/AEquipment/process(es) controlled. Include emission pointdesignations (e.g., E3, E4 from plot plan)N/AMethod of solid waste disposalN/ANature and frequency of routine/preventive maintenanceproceduresN/AProblems experienced with control device within the last fiveyears; how were problems solved?N/AContinuous monitoring method(s) used to monitor ESPperformance, including parameters monitoredN/ADescribe any plans to replace or upgrade ESPN/AFORM C-2AIR POLLUTION CONTROLII. ScrubberNot applicable to thisfacility.For each Scrubber:ScrubberProcess line(s) (identification name/number) N/AEquipment/process(es) controlled. Include emission pointdesignations (e.g., E3, E4 from plot plan)N/ALatitude (decimal degrees, six decimal places)N/ALongitude (decimal degrees, six decimal places)N/AStack or vent height (units)N/AStack or vent diameter (units)N/AManufacturer and modelN/ADate of original installationN/AType (e.g., venturi, orifice)N/AGas flow rate to scrubber (acfm @°F)N/AInlet gas temperature (°F)N/AOutlet gas temperature (°F)N/AInlet grain loading (gr/dscf)N/AOutlet grain loading (gr/dscf)N/AAverage stack opacity (%)N/AWater flow rate to scrubber (gpm) N/APercent of scrubber water from recycled wastewater N/ASource of scrubbing water and type of pretreatment. Substance(s)added as part of pretreatment and amount used (gpmor lbs/hr)N/AHAP composition of wastewater (mg/L) N/AConcentration (mg/L) of dissolved and suspended solids inscrubbing waterN/AScrubbing water temperature (°F)N/ALiquid/gas ratio (gal/103acfm)N/APressure drop across scrubber (in. H2O gauge) N/AAmount of wastewater generated (gpd) N/AAmount of wastewater recycled (gpd) N/AFORM C-2AIR POLLUTION CONTROLII. ScrubberNot applicable to thisfacility.For each Scrubber:ScrubberProcess line(s) (identification name/number) N/AEquipment/process(es) controlled. Include emission pointdesignations (e.g., E3, E4 from plot plan)N/AAmount of wastewater disposed of (gpd) N/AMethod of wastewater disposalN/AQuantity of solid waste collected (lbs/yr) N/AQuantity of solid waste recycled (lbs/yr) N/AQuantity of solid waste disposed of (lbs/yr) N/AMethod of solid waste disposalN/AVendor guarantee on scrubber efficiency (attach copy) N/ANature and frequency of preventive maintenance procedures N/AProblems experienced with control device within the last five years;how were problems solved?N/AContinuous monitoring method(s) used to monitor scrubberperformance, including parameters monitoredN/APlans to replace or upgrade scrubber N/AFORM C-3AIR POLLUTION CONTROLIII. Mechanical CollectorNot applicable to thisfacility.For each Mechanical Collector:Mechanical CollectorProcess line(s) (identification name/number) N/AEquipment/process(es) controlled. Include emission pointdesignations (e.g., E3, E4 from plot plan)N/ALatitude (decimal degrees, six decimal places)N/ALongitude (decimal degrees, six decimal places)N/AStack or vent height (units)N/AStack or vent diameter (units)N/AManufacturer and modelN/ADate of original installationN/AType of mechanical collectorN/AGas flow rate to collector (acfm @°F)N/AInlet gas temperature (°F)N/AOutlet gas temperature (°F)N/AInlet grain loading (gr/dscf)N/AOutlet grain loading (gr/dscf)N/AAverage stack opacity (%)N/AOverall pressure drop (in. H2O gauge) N/AVendor guarantee on mechanical collector efficiency (attachcopy)N/AQuantity of solid waste collected (lbs/yr) N/AQuantity of solid waste recycled (lbs/yr) N/AQuantity of solid waste disposed of (lbs/yr) N/AMethod of solid waste disposal N/ANature and frequency of preventive maintenance procedures N/AProblems experienced with control device within the last fiveyears; how were problems solved?N/AContinuous monitoring method(s) used to monitor performance,including parameters monitoredN/APlans to replace or upgrade mechanical collector N/AFORM C-4AIR POLLUTION CONTROLIV. Fabric FilterFor each Fabric Filter:Fabric Filter 1 Fabric Filter 2Process line(s) (identification name/number) SL1 (bonded) SL1 (bonded)Equipment/process(es) controlled. Include emissionpoint designations (e.g., E3, E4 from plot plan)SL1 Furnace (#1 Melter DustCollector)SL1 Furnace (#2 Melter DustCollector)Latitude (decimal degrees, six decimal places)40.751501740.7514936Longitude (decimal degrees, six decimal places)-111.9958811-111.9958811Stack or vent height (units)76.59 ft. (north stack)76.59 ft. (south stack)Stack or vent diameter (units)1.0 ft. (north stack)1.0 ft. (south stack)Manufacturer and model MikroPul Pulse Jet MikroPul Pulse JetDate of original installation Not known. Acquired facilityin 1995.Not known. Acquired facilityin 1995.Number of compartments 1 1Number of bags per compartment 49 49Filter material and coatings applied P84 Felt/ No Coatings P84 Felt / No CoatingsFabric weight (oz/yd2) 16 oz/yd216 oz/yd2Filter surface area (ft2) 9.43 ft29.43 ft2Gas flow rate to filter (acfm @°F)2,218 acfm @ 166 °F 2,011 acfm @ 122 °FInlet gas temperature (°F)No data available. No data available.Outlet gas temperature (°F)166 °F 122 °FInlet grain loading (gr/dscf) No data available. No data available.Outlet grain loading (gr/dscf) 0.0123 gr/dscf 0.0139 gr/dscfAverage stack opacity (%) <20% <20%Overall pressure drop (in. H2O gauge) 3.5" 3.5"Method and frequency of bag cleaningAutomated air blast based ondifferential pressure.Automated air blast based ondifferential pressure.Vendor guarantee on fabric filter efficiency(attachcopy)None provided. None provided.Quantity of solid waste collected (lbs/yr) N/A(Closed system retunscollected dust to process.)N/A (Closed system retunscollected dust to process.)FORM C-4AIR POLLUTION CONTROLIV. Fabric FilterFor each Fabric Filter:Fabric Filter 1 Fabric Filter 2Process line(s) (identification name/number) SL1 (bonded) SL1 (bonded)Equipment/process(es) controlled. Include emissionpoint designations (e.g., E3, E4 from plot plan)SL1 Furnace (#1 Melter DustCollector)SL1 Furnace (#2 Melter DustCollector)Quantity of solid waste recycled (lbs/yr) N/A(Closed system retunscollected dust to process.)N/A (Closed system retunscollected dust to process.)Quantity of solid waste disposed of (lbs/yr) 0lbs 0 lbsMethod of solid waste disposal N/A N/ANature and frequency of preventive maintenanceproceduresGeneral maintenance repairsas needed. Visualinspections and differentialpressure checks areperformed routinely. Bag orcartridge replacement isperformed as needed.General maintenance repairsas needed. Visualinspections and differentialpressure checks areperformed routinely. Bag orcartridge replacement isperformed as needed.Problems experienced with control device within thelast five years; how were problems solved?Facility is not a Title V facilityand not subject torecordkeeping requirementsof control device problems.Facility is not a Title V facilityand not subject torecordkeeping requirementsof control device problems.Continuous monitoring method(s) used to monitorperformance, including parameters monitoredDifferential Pressure Differential PressurePlans to replace or upgrade fabric filter Nonecurrently approved orscheduled at this time.None currently approved orscheduled at this time.FORM C-5AIR POLLUTION CONTROLV. Thermal IncineratorNot applicable to this facility.For each Thermal Incinerator: Thermal IncineratorProcess line(s) (identification name/number) N/AEquipment/process(es) controlled. Include emissionpoint designations (e.g., E3, E4 from plot plan)N/ALatitude (decimal degrees, six decimal places)N/ALongitude (decimal degrees, six decimal places)N/AStack or vent height (units)N/AStack or vent diameter (units)N/AManufacturer and model N/ADate of original installation N/AFuel type: gas or oil N/AFuel consumption rate (BTU/hr) N/AInlet gas flow rate (acfm @°F)N/AInlet gas temperature (°F)N/ACombustion chamber gas temperature (°F)N/AOutlet gas temperature (°F)N/AInlet grain loading (gr/dscf) N/AOutlet grain loading (gr/dscf) N/AAverage stack opacity (%) N/AExcess air (%)N/AResidence time (sec) at temperature (°F)N/APercent heat recovery N/AVendor guarantee on incinerator efficiency (attachcopy)N/ANature and frequency of preventive maintenanceproceduresN/AProblems experienced with control device within thelast five years; how were problems solved?N/AFORM C-5AIR POLLUTION CONTROLV. Thermal IncineratorNot applicable to this facility.For each Thermal Incinerator: Thermal IncineratorProcess line(s) (identification name/number) N/AEquipment/process(es) controlled. Include emissionpoint designations (e.g., E3, E4 from plot plan)N/AContinuous monitoring method(s) used to monitorincinerator performance, including parameters monitoredN/APlans to replace or upgrade thermal incinerator N/AFORM C-6AIR POLLUTION CONTROLVI. High Velocity Air Filter (HVAF)Not applicable to this facility.For each HVAF:HVAFProcess line(s) (identification name/number) N/AEquipment/process(es) controlled. Include emissionpoint designations (e.g., E3, E4 from plot plan)N/ALatitude (decimal degrees, six decimal places)N/ALongitude (decimal degrees, six decimal places)N/AStack or vent height (units)N/AStack or vent diameter (units)N/AManufacturer and model N/ADate of original installation N/AInlet gas flow rate (acfm @°F)N/AInlet gas temperature (°F)N/AOutlet gas temperature (°F)N/AInlet grain loading (gr/dscf) N/AOutlet grain loading (gr/dscf) N/AAverage stack opacity (%) N/AWater spray pressure (sdig), if applicable N/AWater spray rate (gpm), if applicable N/AFilter face velocity (acfm/ft2)N/AMaximum pressure drop across mat (in. H2O gauge) N/AVendor guarantee on HVAF efficiency (attach copy) N/AMethod and frequency of filter mad advancement N/AAmount of wastewater generated (gpd) N/AAmount of wastewater recycled (gpd) N/AAmount of wastewater disposed of (gpd) N/AMethod of wastewater disposal N/AQuantity of solid waste collected (lbs/yr) N/AFORM C-6AIR POLLUTION CONTROLVI. High Velocity Air Filter (HVAF)Not applicable to this facility.For each HVAF:HVAFProcess line(s) (identification name/number) N/AEquipment/process(es) controlled. Include emissionpoint designations (e.g., E3, E4 from plot plan)N/AQuantity of solid waste recycled (lbs/yr) N/AQuantity of solid waste disposed of (lbs/yr) N/AMethod of solid waste disposal N/ANature and frequency of preventive maintenanceproceduresN/AProblems experienced with control device within thelast five years; how were problems solved?N/AContinuous monitoring method(s) used to monitorHVAF performance, including parameters monitoredN/APlans to replace or upgrade HVAF N/AFORM C-7AIR POLLUTION CONTROLVII. Mist EliminatorNot applicable to this facility.For each Mist Eliminator:Mist EliminatorProcess line(s) (identification name/number) N/AEquipment/process(es) controlled. Include emission pointdesignations (e.g., E3, E4 plot plan)N/ALatitude (decimal degrees, six decimal places)N/ALongitude (decimal degrees, six decimal places)N/AStack or vent height (units)N/AStack or vent diameter (units)N/AManufacturer and modelN/ADate of original installationN/AType of mist eliminatorN/AGas flow rate to mist eliminator (acfm @°F)N/AInlet gas temperature (°F)N/AOutlet gas temperature (°F)N/AInlet grain loading (gr/dscf)N/AOutlet grain loading (gr/dscf)N/AAverage stack opacity (%)N/AVelocity in mist eliminator (ft/sec) N/APressure drop (in. H2O gauge) N/AFor chevron blade mist eliminators:N/ASpacing between blades (in.) N/AWashing frequency of blades N/AFor mesh pad mist eliminators:N/ANumber of pads or elements N/AThickness of pad (in.) or element dimensions N/ADensity of pad, (lb/ft3)N/AWashing frequency of padN/AVendor guarantee on mist eliminator efficiency (attach copy) N/AAmount of wastewater generated (gpd) N/AFORM C-7AIR POLLUTION CONTROLVII. Mist EliminatorNot applicable to this facility.For each Mist Eliminator:Mist EliminatorAmount of wastewater recycled (gpd) N/AAmount of wastewater disposed of (gpd) N/AMethod of wastewater disposal N/AQuantity of solid waste collected (lbs/yr) N/AQuantity of solid waste recycled (lbs/yr) N/AQuantity of solid waste disposed of (lbs/yr) N/AMethod of solid waste disposal N/ANature and frequency of preventive maintenance procedures N/AProblems experienced with control device within the last fiveyears; how were problems solved?N/AContinuous monitoring method(s) used to monitor mist eliminatorperformance, including parameters monitoredN/APlans to replace or upgrade mist eliminator N/AFORM C-8AIR POLLUTION CONTROLVIII. Ventilation SystemFor each Ventilation System:Ventilation System 1Process line(s) (identification name/number)Furnace HallEquipment/process(es) controlled. Include emission pointdesignations (e.g., E3, E4 from plot plan)Fugitive / Furnace VentsLatitude (decimal degrees, six decimal places) 40.7515431 (north) and40.7514761 (south)Longitude (decimal degrees, six decimal places)-111.9957972 (north) and-111.9957983 (south)Stack or vent height (units)55.03 ft.Stack or vent diameter (units)10.50 ft.For general or building ventilation:Ventilation system usedNatural draft system withwall and roof louversAirflow control system used Manually adjustedseasonally.Number of air changes per hour Estimatedat 4-6 airchanges per hour.For unit or local ventilation:Enclosure or hood design usedN/AVolume of enclosure or hoodN/ACapture velocity (ft/sec)N/ADistance between hood and emission source (ft)N/AFORM C-9AIR POLLUTION CONTROLIX. OtherFor each Other Air Pollution Control Device (APCD): Other APCDProcess line(s) (identification name/number) SL1 FormingEquipment/process(es) controlled. Include emission pointdesignations (e.g., E3, E4 from plot plan)SL1 (Bonded)Latitude (decimal degrees, six decimal places)40.7515131Longitude (decimal degrees, six decimal places)-111.9959186Stack or vent height (units)81.28 ftStack or vent diameter (units)4.5 ft.DescriptionDrop-Out BoxesFORM DPROCESS LINE STARTUP AND SHUTDOWNN/A - Facility is not subject to MACT Subpart NNN or other recordkeepingrequirements that provide a method of accurate determination of start-upsand shutdowns.1. For each startup and shutdown (SS) that occurred during the lastfive years, please provide the following information requested in A.through J.A. Using the definitions provided above, indicate whether theevent was a startup or shutdown;N/AB. A description of the event, including identification of theemissions source or sources associated with the startup orshutdown;N/AC. Whether any permit condition was exceededand, if so, whatpermit condition was exceeded;No.D. Whether the event was covered by any contingency plan forcontrolling emissions during startup and shutdown events and, if so,whether the plan was followed; if the plan was notfollowed, why not;No.E. The duration of the event;N/AF. The actions taken to minimize emissions during the event,including the use of any backup control systems;N/AG. Estimates or measurements, if any, of emissions during theevent; if you did not have the ability to quantifyemissions during theevent, please explain why;N/AH. Whether the emission profile of each unitwas different duringstartup and shutdown than during normal operating conditions and, ifso, how emissions were different and why; please provide anysupporting information;No.I. All performance test data collected during each period of SS;the test method used for each event; when the testing wasconducted and why; the test conditions at the timeof testing; andwhether the tests were associated with a routine startup or shutdown;andN/AStartup: 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 DPROCESS LINE STARTUP AND SHUTDOWNN/A - Facility is not subject to MACT Subpart NNN or other recordkeepingrequirements that provide a method of accurate determination of start-upsand shutdowns.J. All monitoring data, including control system parametermonitoring, collected during each period of SS.N/AIf this information is contained in periodic and immediate SS reports(either stand-alone or contained within the periodic excess emissionsreport) submitted to your permitting authority, youmay submit copiesof those reports instead.2. Are there any types of startup or shutdown events that you havebeen able to eliminate? If so, please describe thetype of event andexplain how these events were eliminated.No.3. Please submit a copy of your SS plan if you arerequired todevelop one.N/A4. Please provide all performance test data collected during periodsof SS over the last 5 years. Indicate the test method used for eachevent.N/A5. Please provide all monitoring data, including control systemparameter monitoring, collected during periods of SS over the last 5years.N/A6. Optional: Do you wish to recommend a standardthat would applyduring startup or shutdown? If so, please describethe event to whichthe standard would apply; the recommended standard(this could bean emission limitation, work practice, or operational standard) thatwould apply during the period; the basis for the recommendedstandard; why and how the standard would minimize emissionsduring the event; and how would compliance be determined and/ormonitored.No.FORM EPRESENCE OF AIR POLLUTANTS IN EMISSION POINTSPlease provide any existing emissions information and data coveringhazardous air pollutants (HAP) and particulate matter (PM) for each listedprocess. Identify the appropriate box for which you are providing specificprocess information and/or pollutant emissions data.Melting Furnace Forming Curing CoolingParticulate Matter (PM, PM 2.5, PM Condensable)Chromium Compounds and Hexavalent Chromium (including any Crspeciation data)Other metal HAP (As, Be, Cd, Co, Hg, Mn, Ni, Pb, Sb, Se)Hydrogen Fluoride (HF)Hydrogen Chloride (HCl)FormaldehydePhenolMethanolOther organic HAPThe existing data requested here has been providedto EPA by the industry’s trade association, the NorthAmerican Insulation Manufacturers Association (“NAIMA”). The existing data provided by NAIMA was setforth inNAIMA’s May 5, 2010 letter to EPA. The existing emissions data provided from fiber glass companies includedtest results for the following pollutants: formaldehyde, methanol, phenol, particulate matter, hydrogen fluoride,metals (antimony, arsenic, beryllium, cadmium, chromium, cobalt, lead, manganese, nickel and selenium),mercury and hexavalent chromium. The existing emissions data provided from mineral wool companies includedtest results for the following pollutants: formaldehyde, methanol, phenol, particulate matter, carbonmonoxide,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 industryrepresentatives. In addition to the existing datasubmitted to EPA, extensive new emissions data is being collectedfrom virtually all companies through the “BTEC, Inc. Quality Assurance Project Plan for the Mineral Wool and WoolFiberglass Emissions Test Program.” This Test Program will collect and submit to EPA, through EPA’s ElectronicReporting 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, nickeland selenium), mercury and hexavalent chromium.FORM F-1COSTI. Process Unit (e.g., cupola, curing oven, etc.):For each Process Unit:Process Unit IDProcess Line IDII. Capital CostsBase yearTotal capital cost, including costs for individual pieces, if available.III. Annual Operating CostsBase year (most recent fiscal year)Total annual operating costsMaintenance materials and replacement parts (specify costs by item)Raw materials costsLabor($/yr) for each labor class(hr/hr) for each labor classUtilities (breakdown for each utility)Waste treatment and/or disposalCosts associated with any work practices and pollution preventiontechniques that are employed at your facilitySavings associated with heat recovery and wastewater and/or solid wastereturned to process from APCD (or sold to another user)Indirect costsOther (specify)Please provide the annual report to shareholders orequivalent for the mostrecent fiscal year. If reports are not available,provide annual sales andprofits (or profit margin) for the most recent fiscal year. If company ispublicly owned, please provide a web link to this information.Identify the market range (regional, national, international) of your products.The company objects to this request because it seeks information that is notrelevant to the EPA Administrator's review obligations pursuant to Clean AirAct Section 112(d)(6) and 112(f)(2).FORM F-1COSTThe company objects to this request because it seeks information that is notrelevant to the EPA Administrator's review obligations pursuant to Clean AirAct Section 112(d)(6) and 112(f)(2).Can your product(s) be substituted by another product(s)? If so, please listyour product(s) and substituted product(s).Wool fiberglass insulation comprises the major market forresidential insulation material used in the UnitedStates.The remaining market consists of cellulose (scrapnewspaper) treated to resist fires, spray foam, foamboards, cotton treated to resist fires, and wool treated toresist fires.Wool fiberglass insulation is preferred over thesealternative insulation materials because it is easily,economically, and safety installed in various buildingsettings, has superior fire performance capabilities, and a70-year history of proven performance and durability.FORM F-2COSTI. Air Pollution Control Device (APCD)For each APCD:APCD IDProcess Unit IDII. Capital CostsBase yearAPCD equipment purchase cost and what was includedList the cost for each piece of auxiliary equipment for each APCD notincluded aboveInstallation costLand purchase costTotal capital costMethod of financining APCDRetrofit installationField erected or modularIII. Annual Operating CostsBase year (most recent fiscal year)Maintenance materials and replacement parts (specify costs by item)Raw materials costsLabor($/yr) for each labor class(hr/hr) for each labor classUtilities (breakdown for each utility)Waste treatment and/or disposalIndirect costsOther (specify)The company objects to this request because it seeks information that is notrelevant to the EPA Administrator's review obligations pursuant to Clean AirAct Section 112(d)(6) and 112(f)(2).FORM F-2Total annual operating cost (most recent fiscal year)Attach annual report to shareholders or equivalentfor the most recent fiscalyear. Alternatively, if company is publicly owned,you can provide yourcompany's web link to this information.