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, LLCFacility AddressStreet960 Central ExpresswayCitySanta ClaraStateCaliforniaZip Code95050CountySanta ClaraFacility CoordinatesLatitude (decimal degrees, six decimal places)37.372872Longitude (decimal degrees, six decimal places)121.953794Specific location represented (e.g., front door of main building, centroidof property, etc.)Centroid of PropertyNumber of employees attached to the wool fiberglass manufacturingfacility:208Design capacity of the plant (tons/yr)Type(s) of process(es) (rotary spin, flame attenuation) at this plantRotary SpinOperation schedulehrs/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 Title V Permit A0041. Providedon CD.III. Technical ContactNameMike PettisTechnical Contact TitleISB Environmental LeaderTelephone740-877-7087Facsimile (Fax)740-328-2696EmailMike.Pettis@owenscorning.comFORM A-2FACILITY INFORMATIONIV. OtherIs the facility a major source of HAP?Yes, currently.If No, did the facility take a limit of its potential HAP emissions to avoidclassification as a major source:N/ADoes 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/AFORM 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 numbersO LineM lineType of process line (e.g., rotary spin, flame attenuation) Rotary Spin Rotary SpinMaximum annual production rate (tons/yr)Age of process equipment (yrs)4451Remaining 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%) and Sand (31%).Method(s) of conveying each raw material to furnace/pots Batch raw materials are transported by screw conveyor &bucket elevator to storage silos. Materials from storagesilos are conveyed to the batch mixer via gravity.Mixedbatch is then pneumatically conveyed to storage silosabove each furnace. The batch is then gravity fedinto abatch feeder for distribution across the furnace via a beltconveyor.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)The above listed binder ingredients are metered intobinder mix tanks. Mixed binder is transferred to arecirculating tank. All storage temperatures are ambient.Total holding time is approximately 45 minutes.Total yearly consumption of binder (gal/yr)Cost of binder ($/gal) for most recent year (specify year)Are binder storage and mixing tanks vented tooutside/inside? Binder mix and storage tanks are vented inside.Method of treating vent air from storage andmix tanksN/AEmission control during liquid raw material transfer from vehiclesto storage tanks.N/ADescribe future source reduction plans and schedules toreformulate binders; List each constituent, proportions wt (%), cost($/gal) for reformulationFORM B-3PLANT OPERATIONSIII. Process - Glass Melting FurnaceFor each Glass Melting Furnace:Furnace 1 Furnace 2Process unit identification name/number M Furnace (S-1) O Furnace (S-19)Process line(s) served (identification name/number) M OLatitude (decimal degrees, six decimal places) 37.3731883 (north) and37.3731072 (south)37.3725747 (north) and37.3724828 (south)Longitude (decimal degrees, six decimal places) -121.9519447 (north) and -121.9519417 (south)-121.9519211 (north) and -121.9519175 (south)Stack or vent height (units) 98 ft. 98 ft. (each)Stack or vent diameter (units) 3.83 ft. 3.83 ft. (each)Manufacturer and model Cold Top Cold TopDate of original installation 1959 1966Estimate 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 rebuild N/A N/ACost of typical major rebuild N/A N/ADate of last major rebuild N/A N/APurpose of last major rebuild N/A N/AIncrease or decrease in emissions N/A N/AFuel type: electric, gas, or oil Electric ElectricFORM B-3PLANT OPERATIONSIII. Process - Glass Melting FurnaceFor each Glass Melting Furnace:Furnace 1 Furnace 2Process unit identification name/number M Furnace (S-1) O Furnace (S-19)Process line(s) served (identification name/number) M OFuel consumption rate (KW/ton of glass or Btu/ton ofglass)List HAPs that are in refractory material Chromium Compounds Chromium CompoundsDesign 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.Basic, routine repairs andreplacements are performedweekly for the batch charger.Repairs to the electricalsystems, which includeselectrodes and regulatingtransformers, are completedevery 30 days. Refractoryrepairs are completedinfrequently and only asnecessary.General maintenance activitiesfollow a prescribed schedulethat is detailed in themaintenance tracking system.Basic, routine repairs andreplacements are performedweekly for the batch charger.Repairs to the electricalsystems, which includeselectrodes and regulatingtransformers, are completedevery 30 days. Refractoryrepairs are completedinfrequently and only asnecessary.FORM B-3PLANT OPERATIONSIII. Process - Glass Melting FurnaceFor each Glass Melting Furnace:Furnace 1 Furnace 2Process unit identification name/number M Furnace (S-1) O Furnace (S-19)Process line(s) served (identification name/number) M ODescribe 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 Attenuation Forming Operation 1 Forming Operation 2Process unit identification name/number M Forming (S-2) O Forming (S-20)Process line(s) served (identification name/number) M OLatitude (decimal degrees, six decimal places) 37.3730042 (A), 37.3730033(B), 37.3730028 (C) and37.3730014 (D)37.3724047 (A), 37.3724042(B), 37.3724036 (C) and37.3724033 (D)Longitude (decimal degrees, six decimal places) -121.9520031 (A), -121.9520289 (B), -121.9520550(C) and -121.9520808 (D)-121.9519669 (A), -121.9520278 (B), -121.9520594(C) and -121.9521217 (D)Stack or vent height (units)87 ft. (each) 107.06 ft. (each)Stack or vent diameter (units)2.83 ft. (each) 2.83 ft. (each)Number of fiber forming devices (spinners) per line.Method of attenuating fiber (e.g., air, flame, or air and flame).Indicate type of burner used (if flame).Air and Flame Air and FlameIs there a forehearth between the furnace andthe formingsection?Yes YesMajor 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.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.Frequency of a major rebuild N/A N/ACost of typical major rebuild N/A N/ADate of last major rebuildN/A N/APurpose of last major rebuild N/A N/AFORM B-4PLANT OPERATIONSIV. Process - Forming -- Rotary Spin / Flame AttenuationFor each Forming Operation -- Rotary Spin/Flame Attenuation Forming Operation 1 Forming Operation 2Process unit identification name/number M Forming (S-2) O Forming (S-20)Process line(s) served (identification name/number) M OIncrease or decrease in emissions N/A N/AIf modular, number of modules and plenumsPresence of water overspray and application rate (gpm)Binder applied and application rate (gpm)Other material applied and application rate (gpm) None NoneTemperature of glass fiber when binder is applied (°F)Temperature of binder when applied to fibers(°F)Method of evenly distributing fibers onto forming conveyor Compressed air lapping system Compressed air lapping systemFormed mat thickness (in.)1"-6" as formed, up to 30" onramp.1"-6" as formed, up to 30" onramp.Forming air flow rate (acfm @ °F)Percent of forming air recirculated and percent exhausted None recirculated, 100%exhausted.None recirculated, 100%exhausted.FORM B-4PLANT OPERATIONSIV. Process - Forming -- Rotary Spin / Flame AttenuationFor each Forming Operation -- Rotary Spin/Flame Attenuation Forming Operation 1 Forming Operation 2Process unit identification name/number M Forming (S-2) O Forming (S-20)Process line(s) served (identification name/number) M ONature 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.General 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.FORM B-4PLANT OPERATIONSIV. Process - Forming -- Rotary Spin / Flame AttenuationFor each Forming Operation -- Rotary Spin/Flame Attenuation Forming Operation 1 Forming Operation 2Process unit identification name/number M Forming (S-2) O Forming (S-20)Process line(s) served (identification name/number) M ODescribe process modification(s) since 1999 that reduceemissionsDescribe future source reduction plans and schedules None currently approved orscheduled at this time.None currently approved orscheduled at this time.FORM B-5PLANT OPERATIONSV. Process - CuringFor eachCuring Oven:Curing Oven 1 Curing Oven 2Process unit identification name/number M Curing (S-3) O Curing (S-21)Process line(s) served (identification name/number) M OLatitude (decimal degrees, six decimal places)37.3730881 (1) and 37.3730931(2)37.3725381Longitude (decimal degrees, six decimal places) -121.9524956 (1) and -121.9522978 (2)-121.9524794Stack or vent height (units) 51.04 ft. (1) and37.50 ft. (2) 49.08 ft.Stack or vent diameter (units) 3.58 ft. (1) and 3.92 ft. (2) 7.08 ft.Method of curingManufacturer and model OC Proprietary design OCProprietary designDate of original installation 1959 1966Major 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.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.Frequency of a major rebuild N/A N/ACost of typical major rebuild N/A N/ADate of last major rebuild N/A N/APurpose of last major rebuild N/A N/AIncrease or decrease in emissions N/A N/AFuel type: electric, gas, or oil Natural GasNatural GasFuel consumption rate (KW/hr or BTU/hr)FORM B-5PLANT OPERATIONSV. Process - CuringFor eachCuring Oven:Curing Oven 1 Curing Oven 2Process unit identification name/number M Curing (S-3) O Curing (S-21)Process line(s) served (identification name/number) M OMoisture content wt (%) of formed mat:inlet2.5 - 5% 2.5 - 5%outlet<0.5% <0.5%Air flow rate (acfm @°F) from curing8,300 acfm @ 635 °F (charge),8,450 acfm @ 705 °F(discharge)38,000 acfm @ 600 °FExhaust air temperature (°F)750 °F 750 °FResidence time of product (mins)Binder content of cured product (LOI)Nature 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.General 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.FORM B-5PLANT OPERATIONSV. Process - CuringFor eachCuring Oven:Curing Oven 1 Curing Oven 2Process unit identification name/number M Curing (S-3) O Curing (S-21)Process line(s) served (identification name/number) M ODescribe process modification(s) since 1999 thatreduce emissionsDescribe future source reduction plans andschedulesNone currently approved orscheduled at this time.None currently approved orscheduled at this time.FORM B-6PLANT OPERATIONSVI. Process - CoolingFor eachCooling Operation: Cooling Operation 1 Cooling Operation 2Process unit identification name/number M Cooling (S-4) O Cooling (S-21 and S-22)Process line(s) served (identification name/number) M OLatitude (decimal degrees, six decimal places)37.373084737.3725108Longitude (decimal degrees, six decimal places)-121.9526331-121.9525644Stack or vent height (units)64 ft.64 ft.Stack or vent diameter (units)2.50 ft.2.50 ft.Cooling air flow rate (acfm @°F)20,000 acfm @ 105 °F 6,000 acfm @ 90 °FPercentage of cooling air recirculated (if any) None NoneCooling air temperature (°F) 100 - 120 °F 90 -120 °FNature 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.General 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.Describe process modification(s) since 1999 thatreduce emissionsDescribe future source reduction plans and schedules None currently approved orscheduled at this time.None currently approved orscheduled at this time.FORM 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.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. ScrubberFor each Scrubber:Scrubber 1 Scrubber 2 Scrubber 3Process line(s) (identification name/number) MO OEquipment/process(es) controlled. Include emission pointdesignations (e.g., E3, E4 from plot plan)M Oven (SS) (S-3) O Oven (SS) (S-21) O Cooling (S-22)Latitude (decimal degrees, six decimal places)37.37297437.37355937.3730847Longitude (decimal degrees, six decimal places)-121.952646-121.952608-121.9526331Stack or vent height (units)54 ft.54 ft.64 ft.Stack or vent diameter (units)1.0 ft.1.0 ft.2.50 ft.Manufacturer and modelOC Proprietary Design OC Proprietary Design SchmeigDate of original installation1959 1967 1966Type (e.g., venturi, orifice)Air Action Cyclone Air Action Cyclone VenturiGas flow rate to scrubber (acfm @°F)3,500 acfm @ 110 °F 3,500 acfm @ 110 °F 6,000 acfm @90 °FInlet gas temperature (°F)110 °F 110 °F 100 - 130 °FOutlet gas temperature (°F)110 °F 110 °F 90 - 120 °FInlet grain loading (gr/dscf)No data available. No data available. No data available.Outlet grain loading (gr/dscf)No data available. No data available. 0.015 gr/scf filterableparticulate @4000-10000 acfmAverage stack opacity (%)N/A N/A <20%Water flow rate to scrubber (gpm) 35 gpm 35 gpm50 - 250 gpmPercent of scrubber water from recycled wastewater 100% industrialreclaim wash water.100% industrialreclaim wash water.100% industrialreclaim wash water.Source of scrubbing water and type of pretreatment. Substance(s)added as part of pretreatment and amount used (gpmor lbs/hr)Industrial reclaim washwater system. Nopretreatment.Industrial reclaim washwater system. Nopretreatment.Industrial reclaim washwater system. Nopretreatment.HAP composition of wastewater (mg/L) No data available. No data available. No data available.Concentration (mg/L) of dissolved and suspended solids inscrubbing water<3% <3% <3%Scrubbing water temperature (°F)No data available. No data available. No data available.Liquid/gas ratio (gal/103acfm)No data available. No data available. No data available.FORM C-2AIR POLLUTION CONTROLII. ScrubberFor each Scrubber:Scrubber 1 Scrubber 2 Scrubber 3Process line(s) (identification name/number) MO OEquipment/process(es) controlled. Include emission pointdesignations (e.g., E3, E4 from plot plan)M Oven (SS) (S-3) O Oven (SS) (S-21) O Cooling (S-22)Pressure drop across scrubber (in. H2O gauge) 1-20" 1-20" 1-20"Amount of wastewater generated (gpd) 0 gpd 0 gpd 0 gpdAmount of wastewater recycled (gpd) 72,000 - 360,000gal/day (IWS system)72,000 - 360,000gal/day (IWS system)72,000 - 360,000gal/day (IWS system)Amount of wastewater disposed of (gpd) 0 gpd 0gpd 0 gpdMethod of wastewater disposalN/A N/A N/AQuantity of solid waste collected (lbs/yr)Approximately 900,000lbs/yr solid waste fromIWS system from allsources using IWS.Approximately 900,000lbs/yr solid waste fromIWS system from allsources using IWS.Approximately 900,000lbs/yr solid waste fromIWS system from allsources using IWS.Quantity of solid waste recycled (lbs/yr) NoneNone NoneQuantity of solid waste disposed of (lbs/yr)Approximately 900,000lbs/yr solid waste fromIWS system from allsources using IWS.Approximately 900,000lbs/yr solid waste fromIWS system from allsources using IWS.Approximately 900,000lbs/yr solid waste fromIWS system from allsources using IWS.Method of solid waste disposalLocal Solid WasteLandfillLocal Solid WasteLandfillLocal Solid WasteLandfillVendor guarantee on scrubber efficiency (attach copy) N/A N/A None provided.FORM C-2AIR POLLUTION CONTROLII. ScrubberFor each Scrubber:Scrubber 1 Scrubber 2 Scrubber 3Process line(s) (identification name/number) MO OEquipment/process(es) controlled. Include emission pointdesignations (e.g., E3, E4 from plot plan)M Oven (SS) (S-3) O Oven (SS) (S-21) O Cooling (S-22)Nature and frequency of preventive maintenance procedures General maintenanceactivities follow aprescribed schedulethat is detailed in themaintenance trackingsystem. Nozzles andflow patterns arechecked daily; repairsare completed asneeded. Cleaning isperformed on a cyclematching machinedowntime.General maintenanceactivities follow aprescribed schedulethat is detailed in themaintenance trackingsystem. Nozzles andflow patterns arechecked daily; repairsare completed asneeded. Cleaning isperformed on a cyclematching machinedowntime.General maintenanceactivities follow aprescribed schedulethat is detailed in themaintenance trackingsystem. Nozzles andflow patterns arechecked daily; repairsare completed asneeded. Cleaning isperformed on a cyclematching machinedowntime.Problems experienced with control device within the last five years;how were problems solved?None reported in TitleV deviation reports.None reported in TitleV deviation reports.None reported in TitleV deviation reports.Continuous monitoring method(s) used to monitor scrubberperformance, including parameters monitoredN/A N/A N/APlans to replace or upgrade scrubber None currentlyapproved or scheduledat this time.None currentlyapproved or scheduledat this time.None currentlyapproved or scheduledat this time.FORM 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 2 Fabric Filter 3Process line(s) (identification name/number) MO M and OEquipment/process(es) controlled. Include emissionpoint designations (e.g., E3, E4 from plot plan)M Batch TransporterBin & Silo (S-86)O Batch TransporterBin & Silo (S-87)Batch Mixing (S-57)Latitude (decimal degrees, six decimal places)No data available.No data available.No data available.Longitude (decimal degrees, six decimal places)No data available.No data available.No data available.Stack or vent height (units)No data available.No data available.No data available.Stack or vent diameter (units)No data available.No data available.No data available.Manufacturer and model Consolidated FluidFlow Inc. model R-37-8Consolidated Fluid Flo,Inc. Model # R-37-8.Micro Pulsair Type340512-20Date of original installation 1971 1971 1986Number of compartments 1 1 1Number of bags per compartment 37 37 340Filter material and coatings applied Terytex needled felt Terytex needled felt Polyester HCEFabric weight (oz/yd2)16 16 16Filter surface area (ft2)349 3496405 ft2Gas flow rate to filter (acfm @°F)1,200 acfm @ 105 °F 1,200 acfm @ 110 °F 24,000 acfm @140 °FInlet gas temperature (°F)110 °F 110 °F 140 °FOutlet gas temperature (°F)110 °F 110 °F 135 °FInlet grain loading (gr/dscf) No data available. No data available. No data available.Outlet grain loading (gr/dscf) No data available. No data available. No data available.Average stack opacity (%) <20% <20% <20%Overall pressure drop (in. H2O gauge) 2.5" 2.5" 3.5"Method and frequency of bag cleaning N/A; bagsreplaced asneeded.N/A; bags replaced asneeded.Reverse pulse air flow.Frequency dependanton pressure drop.Vendor guarantee on fabric filter efficiency(attachcopy)None provided. None provided. None provided.FORM C-4AIR POLLUTION CONTROLIV. Fabric FilterFor each Fabric Filter:Process line(s) (identification name/number)Equipment/process(es) controlled. Include emissionpoint 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 modelDate of original installationNumber of compartmentsNumber of bags per compartmentFilter material and coatings appliedFabric weight (oz/yd2)Filter surface area (ft2)Gas flow rate to filter (acfm @°F)Inlet gas temperature (°F)Outlet gas temperature (°F)Inlet grain loading (gr/dscf)Outlet grain loading (gr/dscf)Average stack opacity (%)Overall pressure drop (in. H2O gauge)Method and frequency of bag cleaningVendor guarantee on fabric filter efficiency(attachcopy)Fabric Filter 4M and OBatch Materials Silo &Unloading System (S56)37.3734081-121.9517575 ft.1.17 ft.Micro Pulsair Type1215-8-THW1979132Terytex needled felt16242 ft21,200 acfm @ 105 °F105 °F105 °FNo data available.No data available.<20%2.5"Reverse pulse air flow.Frequency dependanton pressure drop.None provided.FORM C-4AIR POLLUTION CONTROLIV. Fabric FilterFor each Fabric Filter:Fabric Filter 1 Fabric Filter 2 Fabric Filter 3Process line(s) (identification name/number) MO M and OEquipment/process(es) controlled. Include emissionpoint designations (e.g., E3, E4 from plot plan)M Batch TransporterBin & Silo (S-86)O Batch TransporterBin & Silo (S-87)Batch Mixing (S-57)Quantity of solid waste collected (lbs/yr) N/A(Closed systemreturns collected dust toprocess.)N/A (Closed systemreturns collected dust toprocess.)N/A (Closed systemreturns collected dust toprocess.)Quantity of solid waste recycled (lbs/yr) N/A(Closed systemreturns collected dust toprocess.)N/A (Closed systemreturns collected dust toprocess.)N/A (Closed systemreturns collected dust toprocess.)Quantity of solid waste disposed of (lbs/yr) 0lbs 0 lbs 0 lbsMethod of solid waste disposal N/A N/A N/ANature and frequency of preventive maintenanceproceduresGeneral maintenancerepairs as needed.Visual inspections anddifferential pressurechecks are performedroutinely. Bag orcartridge replacementis performed asneeded.General maintenancerepairs as needed.Visual inspections anddifferential pressurechecks are performedroutinely. Bag orcartridge replacementis performed asneeded.General maintenancerepairs as needed.Visual inspections anddifferential pressurechecks are performedroutinely. Bag orcartridge replacementis performed asneeded.Problems experienced with control device within thelast five years; how were problems solved?None reported in Title Vdeviation reports.None reported in Title Vdeviation reports.None reported in Title Vdeviation reports.Continuous monitoring method(s) used to monitorperformance, including parameters monitoredN/A N/A Pressure dropPlans to replace or upgrade fabric filter Nonecurrentlyapproved or scheduledat this time.None currentlyapproved or scheduledat this time.None currentlyapproved or scheduledat this time.FORM C-4AIR POLLUTION CONTROLIV. Fabric FilterFor each Fabric Filter:Process line(s) (identification name/number)Equipment/process(es) controlled. Include emissionpoint designations (e.g., E3, E4 from plot plan)Quantity of solid waste collected (lbs/yr)Quantity of solid waste recycled (lbs/yr)Quantity of solid waste disposed of (lbs/yr)Method of solid waste disposalNature and frequency of preventive maintenanceproceduresProblems experienced with control device within thelast five years; how were problems solved?Continuous monitoring method(s) used to monitorperformance, including parameters monitoredPlans to replace or upgrade fabric filterFabric Filter 4M and OBatch Materials Silo &Unloading System (S56)N/A (Closed systemreturns collected dust toprocess.)N/A (Closed systemreturns collected dust toprocess.)0 lbsN/AGeneral maintenancerepairs as needed.Visual inspections anddifferential pressurechecks are performedroutinely. Bag orcartridge replacementis performed asneeded.None reported in Title Vdeviation reports.Pressure dropNone currentlyapproved or scheduledat this time.FORM C-5AIR POLLUTION CONTROLV. Thermal IncineratorFor each Thermal Incinerator: Thermal Incinerator1 Thermal Incinerator 2 Thermal Incinerator 3Process line(s) (identification name/number) MM OEquipment/process(es) controlled. Include emissionpoint designations (e.g., E3, E4 from plot plan)M Line Oven Charge (S-3) M Line Oven Discharge (S-3)O Line Oven Discharge (S-21)Latitude (decimal degrees, six decimal places)37.373088137.373093137.3725381Longitude (decimal degrees, six decimal places)-121.9524956-121.9522978-121.9524794Stack or vent height (units)51.04 ft.37.50 ft.49.08 ft.Stack or vent diameter (units)3.58 ft.3.92 ft.7.08 ft.Manufacturer and modelOC proprietary design with HirtComb. Co. heat exchangersOC proprietary design with HirtComb. Co. heat exchangersOC proprietary design with HirtComb. Co. heat exchangersDate of original installation 1960 1960 1968Fuel type: gas or oil Natural Gas Natural Gas Natural GasFuel consumption rate (BTU/hr) 4,670,000 BTU/hr 6,000,000 BTU/hr 6,322,900 BTU/hrInlet gas flow rate (acfm @°F)No data available. No data available. No data available.Inlet gas temperature (°F)425 - 450 °F 425 - 450 °F 425 - 450 °FCombustion chamber gas temperature (°F)1,340 °F 1,340 °F 1,340 °FOutlet gas temperature (°F)635 °F 705 °F 625 °FInlet grain loading (gr/dscf) No data available. No data available. No data available.Outlet grain loading (gr/dscf) 0.0019 gr/dscf 0.0020 gr/dscf 0.0079 gr/dscfAverage stack opacity (%) <20% <20% <20%Excess air (%)15% 15% 15%Residence time (sec) at temperature (°F)1.3 seconds at 1350 °F 1.3 seconds at 1350 °F 0.65seconds at 1350 °FPercent heat recovery 68% 68% 68%Vendor guarantee on incinerator efficiency (attachcopy)N/A N/A N/ANature and frequency of preventive maintenanceproceduresAnnual inspections performedper MACT requirement andrepairs made as needed.Annual inspections performedper MACT requirement andrepairs made as needed.Annual inspections performedper MACT requirement andrepairs made as needed.FORM C-5AIR POLLUTION CONTROLV. Thermal IncineratorFor each Thermal Incinerator: Thermal Incinerator1 Thermal Incinerator 2 Thermal Incinerator 3Process line(s) (identification name/number) MM OEquipment/process(es) controlled. Include emissionpoint designations (e.g., E3, E4 from plot plan)M Line Oven Charge (S-3) M Line Oven Discharge (S-3)O Line Oven Discharge (S-21)Problems experienced with control device within thelast five years; how were problems solved?As reported in Title V deviationreports: mechanicalmalfunction / repaired.None reported in Title Vdeviation reports.None reported in Title Vdeviation reports.Continuous monitoring method(s) used to monitorincinerator performance, including parameters monitoredFirebox temperature Firebox temperature Firebox temperaturePlans to replace or upgrade thermal incinerator None currently approved orscheduled at this time.None currently approved orscheduled at this time.None currently approved orscheduled at this time.FORM C-6AIR POLLUTION CONTROLVI. High Velocity Air Filter (HVAF)For each HVAF:HVAF 1 HVAF 2 HVAF 3Process line(s) (identification name/number) MM OEquipment/process(es) controlled. Include emissionpoint designations (e.g., E3, E4 from plot plan)M Line Oven (SS, A-102) (S-3) M Line Oven (HEAF, A-7) (S4)O Line Oven (SS, A-100) (S-21)Latitude (decimal degrees, six decimal places)37.37297437.37308537.372559Longitude (decimal degrees, six decimal places)-121.952646-121.9552633-121.952608Stack or vent height (units)54 ft.64 ft.54 ft.Stack or vent diameter (units)1 ft2.5 ft.1 ft.Manufacturer and model OC Proprietary Design Wheelabrator HEAF OC Proprietary DesignDate of original installation 1959 1974 1967Inlet gas flow rate (acfm @°F)No data available. No data available. No data available.Inlet gas temperature (°F)No data available. No data available. No data available.Outlet gas temperature (°F)96 °F 105 °F 116 °FInlet grain loading (gr/dscf) No data available. No data available. No data available.Outlet grain loading (gr/dscf) 0.0026 gr/dscf 0.0143 gr/dscf 0.0014 gr/dscfAverage stack opacity (%) <20% <20% <20%Water spray pressure (sdig), if applicable Nodata available. No data available. No data available.Water spray rate (gpm), if applicable 20 - 40gpm N/A 20 - 40 gpmFilter face velocity (acfm/ft2)No data available. No data available. No data available.Maximum pressure drop across mat (in. H2O gauge) 30" 25-30" 30"Vendor guarantee on HVAF efficiency (attach copy) N/A None provided. N/AMethod and frequency of filter mad advancement Filters are replaced threetimes per week.Autofeed, as required bydifferential pressure.Filters are replaced threetimes per week.Amount of wastewater generated (gpd) 0 gpd 0 gpd 0 gpdAmount of wastewater recycled (gpd) 100% 100% 100%Amount of wastewater disposed of (gpd) 0 gpd 0gpd 0 gpdMethod of wastewater disposal N/A N/A N/AQuantity of solid waste collected (lbs/yr) 5,500 lbs/yr 74,000 lbs/yr 5,500 lbs/yrFORM C-6AIR POLLUTION CONTROLVI. High Velocity Air Filter (HVAF)For each HVAF:HVAF 1 HVAF 2 HVAF 3Process line(s) (identification name/number) MM OEquipment/process(es) controlled. Include emissionpoint designations (e.g., E3, E4 from plot plan)M Line Oven (SS, A-102) (S-3) M Line Oven (HEAF, A-7) (S4)O Line Oven (SS, A-100) (S-21)Quantity of solid waste recycled (lbs/yr) 0 lbs/yr 0 lbs/yr 0 lbs/yrQuantity of solid waste disposed of (lbs/yr) 5,500 lbs/yr 74,000 lbs/yr 5,500 lbs/yrMethod of solid waste disposal Local Solid Waste Landfill Local Solid Waste Landfill Local Solid Waste LandfillNature and frequency of preventive maintenanceproceduresGeneral maintenance activitiesfollow a prescribed schedulethat is detailed in themaintenance tracking system.Nozzles and flow patterns arechecked daily; repairs arecompleted as needed.Cleaning is performed on acycle matching machinedowntime.General maintenance activitiesfollow a prescribed schedulethat is detailed in themaintenance tracking system.Cleaning is performed on acycle matched to machinedowntime.General maintenance activitiesfollow a prescribed schedulethat is detailed in themaintenance tracking system.Nozzles and flow patterns arechecked daily; repairs arecompleted as needed.Cleaning is performed on acycle matching machinedowntime.Problems experienced with control device within thelast five years; how were problems solved?None reported in Title Vdeviation reports.As reported in Title V deviationreports: high pressure drop /filter change.None reported in Title Vdeviation reports.Continuous monitoring method(s) used to monitorHVAF performance, including parameters monitoredFan amps, pressure dropacross filter media, water flow.Fan amps, pressure dropacross filter media, water flow.Fan amps, pressure dropacross filter media, water flow.Plans to replace or upgrade HVAF None currently approved orscheduled at this time.None currently approved orscheduled at this time.None currently approved orscheduled at this time.FORM 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)Multiple LocationsLongitude (decimal degrees, six decimal places)Multiple LocationsStack or vent height (units)Roof HeightStack or vent diameter (units)Multiple LocationsFor general or building ventilation:Ventilation system usedNatural draft with walland roof louversAirflow control system usedManually adjusted.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): APCD 1 APCD 2Process line(s) (identification name/number) MOEquipment/process(es) controlled. Include emission pointdesignations (e.g., E3, E4 from plot plan)M Forming (S-2) O Forming (S-20)Latitude (decimal degrees, six decimal places) 37.3730042 (A),37.3730033 (B),37.3730028 (C) and37.3730014 (D)37.3724047 (A),37.3724042 (B),37.3724036 (C) and37.3724033 (D)Longitude (decimal degrees, six decimal places) -121.9520031 (A), -121.9520289 (B), -121.9520550 (C) and -121.9520808 (D)-121.9519669 (A), -121.9520278 (B), -121.9520594 (C) and -121.9521217 (D)Stack or vent height (units)87 ft. (each)107.06 ft. (each)Stack or vent diameter (units)2.83 ft. (each)2.83 ft. (each)DescriptionCyclonic Separator Cyclonic SeparatorFORM DPROCESS LINE STARTUP AND SHUTDOWN2005 - 2009 Semi-Annual MACT reports provided on CD.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;As indicated in the 2005 - 2009 Semi-Annual MACT Reports.B. A description of the event, including identification of theemissions source or sources associated with the startup orshutdown;As indicated in the 2005 - 2009 Semi-Annual MACT Reports.C. Whether any permit condition was exceededand, if so, whatpermit condition was exceeded;As indicated in the 2005 - 2009 Semi-Annual MACT Reports.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;As indicated in the 2005 - 2009 Semi-Annual MACT Reports.E. The duration of the event;As indicated in the 2005 - 2009 Semi-Annual MACT Reports.F. The actions taken to minimize emissions during the event,including the use of any backup control systems;As indicated in the 2005 - 2009 Semi-Annual MACT Reports.G. Estimates or measurements, if any, of emissions during theevent; if you did not have the ability to quantifyemissions during theevent, please explain why;As indicated in the 2005 - 2009 Semi-Annual MACT Reports.H. 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;As indicated in the 2005 - 2009 Semi-Annual MACT Reports.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;andNo data available.J. All monitoring data, including control system parametermonitoring, collected during each period of SS.As indicated in the 2005 - 2009 Semi-Annual MACT Reports.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 DPROCESS LINE STARTUP AND SHUTDOWN2005 - 2009 Semi-Annual MACT reports provided on CD.If 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.As indicated in the 2005 - 2009 Semi-Annual MACT Reports.4. Please provide all performance test data collected during periodsof SS over the last 5 years. Indicate the test method used for eachevent.No data available.5. Please provide all monitoring data, including control systemparameter monitoring, collected during periods of SS over the last 5years.As indicated in the 2005 - 2009 Semi-Annual MACT Reports.6. 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 majormarket for residential insulation material used inthe United States. The remaining market consistsof cellulose (scrap newspaper) treated to resistfires, spray foam, foam boards, cotton treated toresist fires, and wool treated to resist fires.Wool fiberglass insulation is preferred over thesealternative insulation materials because it is easily,economically, and safety installed in variousbuilding settings, has superior fire performancecapabilities, and a 70-year history of provenperformance 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 classUtilites (breackdown 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.