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 AddressStreet300 Sunshine Rd.CityKansas CityStateKansasZip Code66115CountyWyandotteFacility CoordinatesLatitude (decimal degrees, six decimal places)39.148578Longitude (decimal degrees, six decimal places)94.614942Specific location represented (e.g., front door of main building, centroidof property, etc.)Centroid of PropertyNumber of employees attached to the wool fiberglass manufacturingfacility:350Design 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 2090010.Provided on 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).4For each process line:Process Line 1Process Line 2Process Line 3Process Line 4Process line identification names or numbers70K5J6U3Type of process line (e.g., rotary spin, flame attenuation) Rotary Spin Rotary Spin Rotary Spin Rotary SpinMaximum annual production rate (tons/yr)Age of process equipment (yrs)35253611Remaining economic life of process line (yrs) N/A.Continuedmaintenance canmaintain indefinite life.N/A. Continuedmaintenance canmaintain indefinite life.N/A. Continuedmaintenance canmaintain indefinite life.N/A. Continuedmaintenance canmaintain indefinitelife.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. 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 Raw material is mixed in batch house andpneumaticallyconveyed to furnace.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 70 Furnace (70FURNACE)(stack 01-03 and 01-04)J5 Furnace (J5FURNACE)(stack 03-05)Process line(s) served (identification name/number) 70 J6 and U3Latitude (decimal degrees, six decimal places) 39.1496769 (stack 01-03) and39.1495919 (stack 01-04)39.1498394Longitude (decimal degrees, six decimal places)-94.6150889 (stack 01-03) and-94.6150906 (stack 01-04)-94.6141128Stack or vent height (units) 67.11 ft (each) 67.57 ft.Stack or vent diameter (units) 4.00 ft. (each)3.00 ft.Manufacturer and model Cold Top Oxy-FuelDate of original installation 1975 1998Estimate 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/AFORM B-3PLANT OPERATIONSIII. Process - Glass Melting FurnaceFor each Glass Melting Furnace:Process unit identification name/numberProcess line(s) served (identification name/number)Latitude (decimal degrees, six decimal places)Longitude (decimal degrees, six decimal places)Stack or vent height (units)Stack or vent diameter (units)Manufacturer and modelDate of original installationEstimate of remaining lifetime (yrs)Major rebuilds:What constitutes a major rebuildFrequency of a major rebuildCost of typical major rebuildDate of last major rebuildPurpose of last major rebuildFurnace 3K5 Furnace (K5FURNACE)(stack 03-25)K539.1496133-94.6141822101.2 ft.3.00 ft.Oxy-Fuel1998N/A. Continued maintenancecan maintain indefinite life.N/AN/AN/AN/AFORM B-3PLANT OPERATIONSIII. Process - Glass Melting FurnaceFor each Glass Melting Furnace:Furnace 1 Furnace 2Process unit identification name/number 70 Furnace (70FURNACE)(stack 01-03 and 01-04)J5 Furnace (J5FURNACE)(stack 03-05)Process line(s) served (identification name/number) 70 J6 and U3Increase or decrease in emissions N/A N/AFuel type: electric, gas, or oil Electric Electric/GasFuel 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.Daily, visible inspection of batchcharge operations, furnacecondition and burner / oxygensupply system. Repairs andreplacements are routinelycompleted when need isidentified. Generalmaintenance activities follow aprescribed schedule that isdetailed in the maintenancetracking system. Refractoryrepairs are completedinfrequently and only asnecessary.FORM B-3PLANT OPERATIONSIII. Process - Glass Melting FurnaceFor each Glass Melting Furnace:Process unit identification name/numberProcess line(s) served (identification name/number)Increase or decrease in emissionsFuel type: electric, gas, or oilFuel consumption rate (KW/ton of glass or Btu/ton ofglass)List HAPs that are in refractory materialDesign 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 maintenanceproceduresFurnace 3K5 Furnace (K5FURNACE)(stack 03-25)K5N/AGas/OxyChromium CompoundsDaily, visible inspection of batchcharge operations, furnacecondition and burner / oxygensupply system. Repairs andreplacements are routinelycompleted when need isidentified. Generalmaintenance activities follow aprescribed schedule that isdetailed in the maintenancetracking system. 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 70 Furnace (70FURNACE)(stack 01-03 and 01-04)J5 Furnace (J5FURNACE)(stack 03-05)Process line(s) served (identification name/number) 70 J6 and U3Describe 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. Batch wettinginstalled.The 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. DEP installed to meetMACT Subpart NNNrequirements.Describe future source reduction plans and schedules None currently approved orscheduled at this time.None currently approved orscheduled at this time.FORM B-3PLANT OPERATIONSIII. Process - Glass Melting FurnaceFor each Glass Melting Furnace:Process unit identification name/numberProcess line(s) served (identification name/number)Describe process modification(s) since 1999 that reduceemissionsDescribe future source reduction plans and schedulesFurnace 3K5 Furnace (K5FURNACE)(stack 03-25)K5The 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.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 70 Forming (70FORMING) J6 Forming (J6FORMING)Process line(s) served (identification name/number)70J6Latitude (decimal degrees, six decimal places) 39.1493044 (stack 01-07),39.1500183 (stack 01-08),39.1494297 (stack 01-09) and39.1494853 (stack 01-10)39.1492742 (stack 04-11),39.1493311 (stack 04-12),39.1494586 (stack 04-14) and39.1494919 (stack 04-16)Longitude (decimal degrees, six decimal places) -94.6147317 (stack 01-07), -94.6147239 (stack 01-08), -94.6148525 (stack 01-09) and -94.6149111 (stack 01-10)-94.6138611 (stack 04-11), -94.6141175 (stack 04-12), -94.6141147 (stack 04-14) and -94.6141353 (stack 04-16)Stack or vent height (units)93.40 ft. (stack 01-07), 100.75ft. (stack 01-08), 99.40 ft. (stack01-09) and 93.40 ft. (stack 01-10)79.18 ft. (stack 04-11), 100.75ft. (stack 04-12), 92.35 ft. (stack04-14) and 88.98 ft. (stack 04-16)Stack or vent diameter (units)4.33 ft. (stack 01-07), 4.58 ft.(stack 01-08), 4.00 ft. (stack 01-09) and 4.33 ft. (stack 01-10)3.42 ft. (stack 04-11), 4.58 ft.(stack 04-12), 3.75 ft. (stack 04-14) and 3.422 ft. (stack 04-16)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:FORM B-4PLANT OPERATIONSIV. Process - Forming -- Rotary Spin / Flame AttenuationFor each Forming Operation -- Rotary Spin/Flame AttenuationProcess unit identification name/numberProcess line(s) served (identification name/number)Latitude (decimal degrees, six decimal places)Longitude (decimal degrees, six decimal places)Stack or vent height (units)Stack or vent diameter (units)Number of fiber forming devices (spinners) per line.Method of attenuating fiber (e.g., air, flame, or air and flame).Indicate type of burner used (if flame).Is there a forehearth between the furnace andthe formingsection?Major rebuilds:Forming Operation 3Forming Operation 4K5 Forming (K5FORMINGNand K5FORMINGS)N/A. Unbonded Loose Fill Line(ULF FORMING) is not rotaryspin / flame attenuation.K5N/A39.1492742 (stack 04-11),39.1493311 (stack 04-12),39.1494586 (stack 04-14) and39.1494919 (stack 04-16)N/A-94.6138611 (stack 04-11), -94.6141175 (stack 04-12), -94.6141147 (stack 04-14) and -94.6141353 (stack 04-16)N/A79.18 ft (stack 04-11), 100.75 ft.(stack 04-12), 92.35 ft. (stack04-14) and 88.98 ft. (stack 04-16)N/A3.42 ft. (stack 04-11), 4.58 ft.(stack 04-12), 3.75 ft. (stack 04-14) and 3.42 ft. (stack 04-16)N/AN/AAir and Flame N/AYes 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 70 Forming (70FORMING) J6 Forming (J6FORMING)Process line(s) served (identification name/number)70J6What 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 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 plenumsPresence of water overspray and application rate (gpm)Binder applied and application rate (gpm)Other material applied and application rate (gpm)NoneNoneTemperature 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 15" onramp.1"-6" as formed, up to 15" 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 AttenuationProcess unit identification name/numberProcess line(s) served (identification name/number)What constitutes a major rebuildFrequency of a major rebuildCost of typical major rebuildDate of last major rebuildPurpose of last major rebuildIncrease or decrease in emissionsIf 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)Temperature of glass fiber when binder is applied (°F)Temperature of binder when applied to fibers(°F)Method of evenly distributing fibers onto forming conveyorFormed mat thickness (in.)Forming air flow rate (acfm @ °F)Percent of forming air recirculated and percent exhaustedForming Operation 3Forming Operation 4K5 Forming (K5FORMINGNand K5FORMINGS)N/A. Unbonded Loose Fill Line(ULF FORMING) is not rotaryspin / flame attenuation.K5N/AThe 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/AN/AN/AN/AN/AN/AN/AN/AN/AN/AN/AN/AN/AN/ANoneN/AN/AN/ACompressed air lapping system N/A1"-6" as formed, up to 15" onramp.N/AN/ANone recirculated, 100%exhausted.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 70 Forming (70FORMING) J6 Forming (J6FORMING)Process line(s) served (identification name/number)70J6Nature 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 AttenuationProcess unit identification name/numberProcess line(s) served (identification name/number)Nature and frequency of routine/preventive maintenanceproceduresForming Operation 3Forming Operation 4K5 Forming (K5FORMINGNand K5FORMINGS)N/A. Unbonded Loose Fill Line(ULF FORMING) is not rotaryspin / flame attenuation.K5N/AGeneral 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 70 Forming (70FORMING) J6 Forming (J6FORMING)Process line(s) served (identification name/number)70J6Describe 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-4PLANT OPERATIONSIV. Process - Forming -- Rotary Spin / Flame AttenuationFor each Forming Operation -- Rotary Spin/Flame AttenuationProcess unit identification name/numberProcess line(s) served (identification name/number)Describe process modification(s) since 1999 that reduceemissionsDescribe future source reduction plans and schedulesForming Operation 3Forming Operation 4K5 Forming (K5FORMINGNand K5FORMINGS)N/A. Unbonded Loose Fill Line(ULF FORMING) is not rotaryspin / flame attenuation.K5N/AN/ANone currently approved orscheduled at this time.N/AFORM B-5PLANT OPERATIONSV. Process - CuringFor eachCuring Oven:Curing Oven 1Curing Oven 2Process unit identification name/number 70 Curing (70OVEN) K5 Curing (K5OVEN)Process line(s) served (identification name/number) 70 K5Latitude (decimal degrees, six decimal places) 39.1494136 (charge) and39.1491536 (discharge)39.1490925 (charge) and39.1487989 (discharge)Longitude (decimal degrees, six decimal places) -94.6149364 (charge) and -94.6147897 (discharge)-94.6138017 (charge) and -94.6138078 (discharge)Stack or vent height (units) 42.27 ft. (charge) and 37.84 ft.(discharge)40.50 ft. (charge) and 45.00 ft.(discharge)Stack or vent diameter (units) 1.66 ft. (charge) and 2.0 ft.(discharge)2.5 ft. (each) and 1.83 ft.(discharge)Method of curingManufacturer and modelOC Proprietary DesignOC Proprietary DesignDate of original installation19751985Major rebuilds:What constitues 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 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 GasNatural GasFuel consumption rate (KW/hr or BTU/hr)FORM B-5PLANT OPERATIONSV. Process - CuringFor eachCuring Oven:Process unit identification name/numberProcess line(s) served (identification name/number)Latitude (decimal degrees, six decimal places)Longitude (decimal degrees, six decimal places)Stack or vent height (units)Stack or vent diameter (units)Method of curingManufacturer and modelDate of original installationMajor rebuilds:What constitues a major rebuildFrequency of a major rebuildCost of typical major rebuildDate of last major rebuildPurpose of last major rebuildIncrease or decrease in emissionsFuel type: electric, gas, or oilFuel consumption rate (KW/hr or BTU/hr)Curing Oven 3Curing Oven 4J6 Curing (J6OVEN) N/A - U3 line (unbonded loosefill) does not have curing.J6 N/A-94.6140550 (charge) and -94.6141042 (discharge)N/A39.1492933 (charge) and39.1491664 (discharge)N/A48.50 ft. (charge) and 35.58 ft.(discharge)N/A1.6 ft. (each) N/AN/AOC Proprietary DesignN/A1985N/AThe 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/AN/AN/AN/AN/AN/AN/AN/AN/AN/AN/ANatural GasN/AN/AFORM B-5PLANT OPERATIONSV. Process - CuringFor eachCuring Oven:Curing Oven 1Curing Oven 2Process unit identification name/number 70 Curing (70OVEN) K5 Curing (K5OVEN)Process line(s) served (identification name/number) 70 K5Moisture content wt (%) of formed mat:inlet2.5 - 5%2.5 - 5%outlet<0.5%<0.5%Air flow rate (acfm @°F) from curing19,000 acfm @ 130 °F20,200 acfm @ 145 °FExhaust air temperature (°F)130 °F145 °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:Process unit identification name/numberProcess line(s) served (identification name/number)Moisture content wt (%) of formed mat:inletoutletAir flow rate (acfm @°F) from curingExhaust air temperature (°F)Residence time of product (mins)Binder content of cured product (LOI)Nature and frequency of routine/preventivemaintenance proceduresCuring Oven 3Curing Oven 4J6 Curing (J6OVEN) N/A - U3 line (unbonded loosefill) does not have curing.J6 N/A2.5 - 5%N/A<0.5%N/A21,200 acfm @ 140 °FN/A140 °FN/AN/AN/AGeneral 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 70 Curing (70OVEN) K5 Curing (K5OVEN)Process line(s) served (identification name/number) 70 K5Describe 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-5PLANT OPERATIONSV. Process - CuringFor eachCuring Oven:Process unit identification name/numberProcess line(s) served (identification name/number)Describe process modification(s) since 1999 thatreduce emissionsDescribe future source reduction plans andschedulesCuring Oven 3Curing Oven 4J6 Curing (J6OVEN) N/A - U3 line (unbonded loosefill) does not have curing.J6 N/AN/ANone currently approved orscheduled at this time.N/AFORM B-6PLANT OPERATIONSVI. Process - CoolingFor eachCooling Operation: Cooling Operation 1 Cooling Operation 2 Cooling Operation 3Process unit identification name/number 70 Cooling (70COOLING) K5 Cooling (K5COOLING) J6 Cooling (J6COOLING)Process line(s) served (identification name/number) 70 K5 J6Latitude (decimal degrees, six decimal places) 39.1490225 (stack 17-08) and39.1488675 (stack 17-12)39.1486992 (07-16) and39.1486250 (07-17)39.1489569 (stack 08-12) and39.1489214 (stack 09-10)Longitude (decimal degrees, six decimal places)-94.6150164 (stack 17-08) and-94.6151325 (stack 17-12)-94.6139772 (07-16) and -94.6139789 (07-17)-94.6140953 (stack 08-12) and-94.6141789 (stack 09-10)Stack or vent height (units) 33.39 ft.(stack 17-08) and35.42 ft. (stack 17-12)34 ft. (07-16) and 33 ft. (07-17) 42.30 ft. (coolingstack north)and 39.00 ft. (cooling stacksouth)Stack or vent diameter (units) 2.08 ft. (stack17-08) and 1.65ft. (stack 17-12)3.0 ft. (each) 3.08 ft. x 3.25 ft. (each)Cooling air flow rate (acfm @°F)38,400 acfm @ 77 °F 35,860 acfm @ 90 °F 36,700 acfm@ 75 °FPercentage of cooling air recirculated (if any) None None NoneCooling air temperature (°F) 70 - 120 °F 85 -120 °F 70 - 120 °FFORM B-6PLANT OPERATIONSVI. Process - CoolingFor eachCooling Operation:Process unit identification name/numberProcess line(s) served (identification name/number)Latitude (decimal degrees, six decimal places)Longitude (decimal degrees, six decimal places)Stack or vent height (units)Stack or vent diameter (units)Cooling air flow rate (acfm @°F)Percentage of cooling air recirculated (if any)Cooling air temperature (°F)Cooling Operation 4N/A - U3 line (unbonded loosefill) does not have cooling.N/AN/AN/AN/AN/AN/AN/AN/AFORM B-6PLANT OPERATIONSVI. Process - CoolingFor eachCooling Operation: Cooling Operation 1 Cooling Operation 2 Cooling Operation 3Process unit identification name/number 70 Cooling (70COOLING) K5 Cooling (K5COOLING) J6 Cooling (J6COOLING)Process line(s) served (identification name/number) 70 K5 J6Nature 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.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.None currently approved orscheduled at this time.FORM B-6PLANT OPERATIONSVI. Process - CoolingFor eachCooling Operation:Process unit identification name/numberProcess line(s) served (identification name/number)Nature and frequency of routine/preventivemaintenance proceduresDescribe process modification(s) since 1999 thatreduce emissionsDescribe future source reduction plans and schedulesCooling Operation 4N/A - U3 line (unbonded loosefill) does not have cooling.N/AN/AN/AN/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.FORM C-1AIR POLLUTION CONTROLI. Electrostatic Precipitator (ESP)For each ESP:ESP 1ESP 2Process line(s) (identification name/number)70J5Equipment/process(es) controlled. Include emission pointdesignations (e.g., E3, E4 from plot plan)70 Forming with WEP(70FORMING and 70WEPB)(stack 01-08)J5 Furnace with DEP(J5FURNACE and J5DEP)(stack 03-01)Latitude (decimal degrees, six decimal places)39.150018339.1496172Longitude (decimal degrees, six decimal places)-94.6147239-94.6142747Stack or vent height (units)100.75 ft.92.92 ft.Stack or vent diameter (units)4.58 ft.3 ft.Manufacturer and modelAlstom Power FAV 15 15 3OH Alstom Power 3x45f-35-40Date of original installation19981998Number of collection plates and configuration38,38,76/Field90/field,Gas flow rate to ESP (acfm @°F)41,080 acfm @ 101 °F26,733 acfm @ 484 °FInlet gas temperature (°F)101 °F484 °FOutlet gas temperature (°F)99 °F462 °FInlet grain loading (gr/dscf)0.0228 gr/dscf0.2582 gr/dscfOutlet grain loading (gr/dscf)0.0010 gr/dscf0.0020 gr/dscfAverage stack opacity (%)<20%<20%Pressure drop across ESP (in. H2O gauge) 1" 3"Plate area (ft2)15,501 16,276Vendor guarantee on ESP efficiency (attach copy)Yes. Provided on CD.Yes. Provided on CD.Method of plate cleaning and frequency Water.Continuously flows. Rappers. Cleaning basedmonitoring parameters.Flow rate of plate wash water to ESP (gpm), if applicable200 - 300 gpmN/ATemperature of plate wash water to ESP (°F), if applicable100°FN/ASource of plate wash water used for cleaning,if applicableRecirculationN/AConcentration (mg/l) of dissolved and suspended solids in platewash water, if applicable0.09 - 0.314 N/AConditioning agents used and amounts (in gpmor lbs/hr), ifapplicableNone NoneAmount of wastewater generated (gpd), if applicable 7,200 gpd blow down to sewer 7,200 gpd blow down to sewerAmount of wastewater recycled (gpd), if applicableNoneNoneFORM C-1AIR POLLUTION CONTROLI. Electrostatic Precipitator (ESP)For each ESP:Process line(s) (identification name/number)Equipment/process(es) controlled. Include emission pointdesignations (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 collection plates and configurationGas flow rate to ESP (acfm @°F)Inlet gas temperature (°F)Outlet gas temperature (°F)Inlet grain loading (gr/dscf)Outlet grain loading (gr/dscf)Average stack opacity (%)Pressure drop across ESP (in. H2O gauge)Plate area (ft2)Vendor guarantee on ESP efficiency (attach copy)Method of plate cleaning and frequencyFlow rate of plate wash water to ESP (gpm), if applicableTemperature of plate wash water to ESP (°F), if applicableSource of plate wash water used for cleaning,if applicableConcentration (mg/l) of dissolved and suspended solids in platewash water, if applicableConditioning agents used and amounts (in gpmor lbs/hr), ifapplicableAmount of wastewater generated (gpd), if applicableAmount of wastewater recycled (gpd), if applicableESP 3ESP 4J6K5J6 Forming with WEP(J6FORMING and J6WEPB)(stack 04-18)K5 Furnace with DEP(K5FURNACE and K5DEP)(stack 03-25)39.150017239.1498394-94.6146356-94.6141128100.75 ft.101.2 ft.4.58 ft.3 ft.Alstom Power FAV 15 15 3OH Alstom Power 3x45f-35-401998199838,38,76/Field90/field,31,207 acfm @ 100 °F27,538 acfm @ 457 °F100 °F484 °F99 °F457 °F0.0142 gr/dscf0.8337 gr/dscf0.0011 gr/dscf0.0164 gr/dscf<20%<20%1" 3"15,501 16,276Yes. Provided on CD.Yes. Provided on CD.Water. Continuously flows. Rappers. Cleaning basedmonitoring parameters.200 - 300 gpmN/A100°FN/ARecirculationN/A0.09 - 0.314 N/ANone None7,200 gpd blow down to sewer 7,200 gpd blow down tosewerNoneNoneFORM C-1AIR POLLUTION CONTROLI. Electrostatic Precipitator (ESP)For each ESP:Process line(s) (identification name/number)Equipment/process(es) controlled. Include emission pointdesignations (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 collection plates and configurationGas flow rate to ESP (acfm @°F)Inlet gas temperature (°F)Outlet gas temperature (°F)Inlet grain loading (gr/dscf)Outlet grain loading (gr/dscf)Average stack opacity (%)Pressure drop across ESP (in. H2O gauge)Plate area (ft2)Vendor guarantee on ESP efficiency (attach copy)Method of plate cleaning and frequencyFlow rate of plate wash water to ESP (gpm), if applicableTemperature of plate wash water to ESP (°F), if applicableSource of plate wash water used for cleaning,if applicableConcentration (mg/l) of dissolved and suspended solids in platewash water, if applicableConditioning agents used and amounts (in gpmor lbs/hr), ifapplicableAmount of wastewater generated (gpd), if applicableAmount of wastewater recycled (gpd), if applicableESP 5ESP 6K5K5K5 Forming with WEP(K5FORMING and K5WEPC)(stack 04-13)K5 Forming with WEP(K5FORMING and K5WEPD)(stack 04-15)39.150015039.1500161-94.6144594-94.6145475100.75 ft.80.85 ft.4.58 ft.4.58 ft.Alstom Power FAV 15 15 3OH Alstom Power FAV 15 15 3OH1998199838,38,76/Field38,38,76/Field36,620 acfm @ 91 °F32,633 acfm @ 93 °F91 °F93 °F98 °F98 °F0.0191 gr/dscf0.0177 gr/dscf0.0001 gr/dscf0.0013 gr/dscf<20%<20%1" 1"15,501 15,501Yes. Provided on CD.Yes. Provided on CD.Water. Flush system. Water. Flush system.200 - 300 gpm200 - 300 gpm100°F100°FRecirculationRecirculation0.09 - 0.314 0.09 - 0.314None None7,200 gpd blow down to sewer 7,200 gpd blow down tosewerNoneNoneFORM C-1AIR POLLUTION CONTROLI. Electrostatic Precipitator (ESP)For each ESP:ESP 1ESP 2Process line(s) (identification name/number)70J5Equipment/process(es) controlled. Include emission pointdesignations (e.g., E3, E4 from plot plan)70 Forming with WEP(70FORMING and 70WEPB)(stack 01-08)J5 Furnace with DEP(J5FURNACE and J5DEP)(stack 03-01)Amount of wastewater disposed of (gpd), if applicable 7,200 gpd blow down to sewer 7,200 gpd blowdown to sewerMethod of wastewater disposal, if applicableCity sewer systemCity sewer systemQuantity of solid waste collected (lbs/yr) 0 lbs 1,000 - 1,500 lbs. Smallquantities of DEP residuebecomes contaminated in theprocess and must be disposed.Quantity of solid waste recycled (lbs/yr)0 lbs0 lbsQuantity of solid waste disposed of (lbs/yr)0 lbs1,000 - 1,500 lbsMethod of solid waste disposalN/AHazardous Waste LandfillNature and frequency of routine/preventive maintenanceproceduresGeneral maintenance activitiesfollow a prescribed schedulethat is detailed in themaintenance tracking system.Systems are continuouslymonitored and notificationsoccur that initiate maintenance.SIR repair and replacement isconducted as needed.Electrode replacement occurson a a12-15 year cycle.General maintenance activitiesfollow a prescribed schedulethat is detailed in themaintenance tracking system.Systems are continuouslymonitored and notificationsoccur that initiate maintenance.SIR repair and replacement isconducted as needed.Electrode replacement occurson a a12-15 year cycle.Problems experienced with control device within the last fiveyears; how were problems solved?As reported in Title V deviationreports: electrical malfunctions /repaired; and mechanicalmalfunctions / repaired.As reported in Title V deviationreports: electrical malfunctions /repaired; and mechanicalmalfunctions / repaired.FORM C-1AIR POLLUTION CONTROLI. Electrostatic Precipitator (ESP)For each ESP:Process line(s) (identification name/number)Equipment/process(es) controlled. Include emission pointdesignations (e.g., E3, E4 from plot plan)Amount of wastewater disposed of (gpd), if applicableMethod of wastewater disposal, if applicableQuantity 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 routine/preventive maintenanceproceduresProblems experienced with control device within the last fiveyears; how were problems solved?ESP 3ESP 4J6K5J6 Forming with WEP(J6FORMING and J6WEPB)(stack 04-18)K5 Furnace with DEP(K5FURNACE and K5DEP)(stack 03-25)7,200 gpd blow down to sewer 7,200 gpd blow down tosewerCity sewer systemCity sewer system0 lbs 1,000 - 1,500 lbs. Smallquantities of DEP residuebecomes contaminated in theprocess and must be disposed.0 lbs0 lbs0 lbs1,000 - 1,500 lbsN/AHazardous Waste LandfillGeneral maintenance activitiesfollow a prescribed schedulethat is detailed in themaintenance tracking system.Systems are continuouslymonitored and notificationsoccur that initiate maintenance.SIR repair and replacement isconducted as needed.Electrode replacement occurson a a12-15 year cycle.General maintenance activitiesfollow a prescribed schedulethat is detailed in themaintenance tracking system.Systems are continuouslymonitored and notificationsoccur that initiate maintenance.SIR repair and replacement isconducted as needed.Electrode replacement occurson a a12-15 year cycle.As reported in Title V deviationreports: electrical malfunctions /repaired; and restricted waterflow / repair.As reported in Title V deviationreports: electrical malfunctions /repaired; and mechanicalmalfunctions / repaired.FORM C-1AIR POLLUTION CONTROLI. Electrostatic Precipitator (ESP)For each ESP:Process line(s) (identification name/number)Equipment/process(es) controlled. Include emission pointdesignations (e.g., E3, E4 from plot plan)Amount of wastewater disposed of (gpd), if applicableMethod of wastewater disposal, if applicableQuantity 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 routine/preventive maintenanceproceduresProblems experienced with control device within the last fiveyears; how were problems solved?ESP 5ESP 6K5K5K5 Forming with WEP(K5FORMING and K5WEPC)(stack 04-13)K5 Forming with WEP(K5FORMING and K5WEPD)(stack 04-15)7,200 gpd blow down to sewer 7,200 gpd blow down tosewerCity sewer systemCity sewer system0 lbs 0 lbs0 lbs0 lbs0 lbs0 lbsN/AN/AGeneral maintenance activitiesfollow a prescribed schedulethat is detailed in themaintenance tracking system.Systems are continuouslymonitored and notificationsoccur that initiate maintenance.SIR repair and replacement isconducted as needed.Electrode replacement occurson a a12-15 year cycle.General maintenance activitiesfollow a prescribed schedulethat is detailed in themaintenance tracking system.Systems are continuouslymonitored and notificationsoccur that initiate maintenance.SIR repair and replacement isconducted as needed.Electrode replacement occurson a a12-15 year cycle.As reported in Title V deviationreports: electrical malfunctions /repaired; mechanicalmalfunctions / repaired; andrestricted water flow / repair.As reported in Title V deviationreports: electrical malfunctions /repaired; mechanicalmalfunctions / repaired; andrestricted water flow / repair.FORM C-1AIR POLLUTION CONTROLI. Electrostatic Precipitator (ESP)For each ESP:ESP 1ESP 2Process line(s) (identification name/number)70J5Equipment/process(es) controlled. Include emission pointdesignations (e.g., E3, E4 from plot plan)70 Forming with WEP(70FORMING and 70WEPB)(stack 01-08)J5 Furnace with DEP(J5FURNACE and J5DEP)(stack 03-01)Continuous monitoring method(s) used to monitor ESPperformance, including parameters monitoredSecondary voltage andamperage of 3rd field.Secondary voltage andamperage of 3rd field.Describe any plans to replace or upgrade ESP None currently approved orscheduled at this time.None currently approved orscheduled at this time.FORM C-1AIR POLLUTION CONTROLI. Electrostatic Precipitator (ESP)For each ESP:Process line(s) (identification name/number)Equipment/process(es) controlled. Include emission pointdesignations (e.g., E3, E4 from plot plan)Continuous monitoring method(s) used to monitor ESPperformance, including parameters monitoredDescribe any plans to replace or upgrade ESPESP 3ESP 4J6K5J6 Forming with WEP(J6FORMING and J6WEPB)(stack 04-18)K5 Furnace with DEP(K5FURNACE and K5DEP)(stack 03-25)Secondary voltage andamperage of 3rd field.Secondary voltage andamperage of 3rd field.None currently approved orscheduled at this time.None currently approved orscheduled at this time.FORM C-1AIR POLLUTION CONTROLI. Electrostatic Precipitator (ESP)For each ESP:Process line(s) (identification name/number)Equipment/process(es) controlled. Include emission pointdesignations (e.g., E3, E4 from plot plan)Continuous monitoring method(s) used to monitor ESPperformance, including parameters monitoredDescribe any plans to replace or upgrade ESPESP 5ESP 6K5K5K5 Forming with WEP(K5FORMING and K5WEPC)(stack 04-13)K5 Forming with WEP(K5FORMING and K5WEPD)(stack 04-15)Secondary voltage andamperage of 3rd field.Secondary voltage andamperage of 3rd field.None currently approved orscheduled at this time.None currently approved orscheduled at this time.FORM C-2AIR POLLUTION CONTROLII. ScrubberFor each Scrubber:Scrubber 1 Scrubber 2 Scrubber 3Process line(s) (identification name/number) 70 70 K5Equipment/process(es) controlled. Include emission pointdesignations (e.g., E3, E4 from plot plan)70 Cooling (70COOLINGand 70SCRUBBER001)(Stack 17-08)70 Cooling (70COOLINGand 70SCRUBBER002)(Stack 17-12)K5 Cooling (K5COOLINGand K5SCRUBBER001)(Stack 07-16)Latitude (decimal degrees, six decimal places) 39.1490225 (stack 17-08) 39.1488675 (stack 17-12) 39.1486992 (stack 07-16)Longitude (decimal degrees, six decimal places) -94.6150164 (stack 17-08) -94.6151325 (stack 17-12) -94.6139772 (stack 07-16)Stack or vent height (units)33.39 ft.35.52 ft.34 ftStack or vent diameter (units)2.08 ft. 1.67 ft. 3 ft.Manufacturer and modelMonroe Environmental Monroe Environmental Monroe EnvironmentalDate of original installation1975 1975 1985Type (e.g., venturi, orifice)Venturi Venturi VenturiGas flow rate to scrubber (acfm @°F)29,000 acfm @ 72 °F 9,426 acfm @ 76 °F 19,903 acfm@ 90 °FInlet gas temperature (°F)100 - 120 °F 100 - 120 °F 100 - 120 °FOutlet gas temperature (°F)80 - 120 °F 80 - 120 °F 80 - 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. 0.0079 gr/dscfAverage stack opacity (%)<20% <20% <20%Water flow rate to scrubber (gpm) 200 - 500 gpm 200 - 500 gpm 450 - 500 gpmPercent of scrubber water from recycled wastewater 100% 100% 100%Source of scrubbing water and type of pretreatment. Substance(s)added as part of pretreatment and amount used (gpmor lbs/hr)Industrial Reclaim ClearWater System. Nopretreatment.Industrial Reclaim ClearWater System. Nopretreatment.Industrial Reclaim ClearWater System. Nopretreatment.HAP composition of wastewater (mg/L) 100 - 150mg/L 100 - 150 mg/L 100 - 150 mg/LConcentration (mg/L) of dissolved and suspended solids inscrubbing waterNo data available. No data available. No data available.Scrubbing water temperature (°F)80 - 110 °F 80 - 110 °F 80 - 110 °FLiquid/gas ratio (gal/103acfm)No data available. No data available. No data available.FORM C-2AIR POLLUTION CONTROLII. ScrubberFor each Scrubber:Process line(s) (identification name/number)Equipment/process(es) controlled. Include emission pointdesignations (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 installationType (e.g., venturi, orifice)Gas flow rate to scrubber (acfm @°F)Inlet gas temperature (°F)Outlet gas temperature (°F)Inlet grain loading (gr/dscf)Outlet grain loading (gr/dscf)Average stack opacity (%)Water flow rate to scrubber (gpm)Percent of scrubber water from recycled wastewaterSource of scrubbing water and type of pretreatment. Substance(s)added as part of pretreatment and amount used (gpmor lbs/hr)HAP composition of wastewater (mg/L)Concentration (mg/L) of dissolved and suspended solids inscrubbing waterScrubbing water temperature (°F)Liquid/gas ratio (gal/103acfm)Scrubber 4 Scrubber 5 Scrubber 6K5 J6 J6K5 Cooling (K5COOLINGand K5SCRUBBER002)(Stack 07-17)J6 Cooling (J6COOLINGand J6SCRUBBER001)(Stack 08-12)J6 Cooling (J6COOLINGand J6SCRUBBER002)(Stack 09-10)39.1486250 (stack 07-17) 39.1489569 (stack 08-12) 39.1489214 (stack 09-10)-94.6139789 (stack 07-17) -94.6140953 (stack 08-12)-94.6141789 (stack 09-10)33 ft.42.3 ft.39 ft.3 ft. 3.25 ft. x 3.08 ft.(rectangular)3.42 ft.Monroe Environmental Monroe Environmental Monroe Environmental1985 1994 1994Venturi Venturi Venturi15,957 acfm @ 90 °F 36,694 acfm @ 75 °F No data available.100 - 120 °F 100 - 120 °F 100 - 120 °F80 - 120 °F 80 - 120 °F 80 - 120 °FNo data available. No data available. No data available.0.0028 gr/dscf No data available. No data available.<20% <20% <20%450 - 500 gpm 337 - 631 gpm 337 - 631 gpm100% 100% 100%Industrial Reclaim ClearWater System. Nopretreatment.Industrial Reclaim ClearWater System. Nopretreatment.Industrial Reclaim ClearWater System. Nopretreatment.100 - 150 mg/L 100 - 150 mg/L 100 - 150 mg/LNo data available. No data available. No data available.80 - 110 °F 80 - 110 °F 80 - 110 °FNo 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) 70 70 K5Equipment/process(es) controlled. Include emission pointdesignations (e.g., E3, E4 from plot plan)70 Cooling (70COOLINGand 70SCRUBBER001)(Stack 17-08)70 Cooling (70COOLINGand 70SCRUBBER002)(Stack 17-12)K5 Cooling (K5COOLINGand K5SCRUBBER001)(Stack 07-16)Pressure drop across scrubber (in. H2O gauge) 4 - 12" 4 - 12" 4 - 12"Amount of wastewater generated (gpd) 0 gpd (infrequentdischarges)0 gpd (infrequentdischarges)0 gpdAmount of wastewater recycled (gpd) 100% 100% 100%Amount of wastewater disposed of (gpd) 0 gpd (infrequentdischarges)0 gpd (infrequentdischarges)0 gpdMethod of wastewater disposalN/A N/A N/AQuantity of solid waste collected (lbs/yr) 220,000 - 300,000 lbs (allsources - wash watersystem)220,000 - 300,000 lbs (allsources - wash watersystem)220,000 - 300,000 lbs (allsources - wash watersystem)Quantity of solid waste recycled (lbs/yr) 0 lbs 0 lbs 0 lbsQuantity of solid waste disposed of (lbs/yr) 220,000 - 300,000 lbs (allsources - wash watersystem)220,000 - 300,000 lbs (allsources - wash watersystem)220,000 - 300,000 lbs (allsources - wash watersystem)Method of solid waste disposalLocal Solid Waste Landfill Local Solid Waste Landfill Local Solid Waste LandfillVendor guarantee on scrubber efficiency (attach copy) None provided. None provided. None provided.FORM C-2AIR POLLUTION CONTROLII. ScrubberFor each Scrubber:Process line(s) (identification name/number)Equipment/process(es) controlled. Include emission pointdesignations (e.g., E3, E4 from plot plan)Pressure drop across scrubber (in. H2O gauge)Amount of wastewater generated (gpd)Amount of wastewater recycled (gpd)Amount of wastewater disposed of (gpd)Method of wastewater disposalQuantity 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 disposalVendor guarantee on scrubber efficiency (attach copy)Scrubber 4 Scrubber 5 Scrubber 6K5 J6 J6K5 Cooling (K5COOLINGand K5SCRUBBER002)(Stack 07-17)J6 Cooling (J6COOLINGand J6SCRUBBER001)(Stack 08-12)J6 Cooling (J6COOLINGand J6SCRUBBER002)(Stack 09-10)4 - 12" 4 - 12" 4 - 12"0 gpd 0 gpd 0 gpd100% 100% 100%0 gpd 0 gpd 0 gpdN/A N/A N/A220,000 - 300,000 lbs (allsources - wash watersystem)220,000 - 300,000 lbs (allsources - wash watersystem)220,000 - 300,000 lbs (allsources - wash watersystem)0 lbs 0 lbs 0 lbs220,000 - 300,000 lbs (allsources - wash watersystem)220,000 - 300,000 lbs (allsources - wash watersystem)220,000 - 300,000 lbs (allsources - wash watersystem)Local Solid Waste Landfill Local Solid Waste Landfill Local Solid Waste LandfillNone provided. None provided. None provided.FORM C-2AIR POLLUTION CONTROLII. ScrubberFor each Scrubber:Scrubber 1 Scrubber 2 Scrubber 3Process line(s) (identification name/number) 70 70 K5Equipment/process(es) controlled. Include emission pointdesignations (e.g., E3, E4 from plot plan)70 Cooling (70COOLINGand 70SCRUBBER001)(Stack 17-08)70 Cooling (70COOLINGand 70SCRUBBER002)(Stack 17-12)K5 Cooling (K5COOLINGand K5SCRUBBER001)(Stack 07-16)Nature and frequency of preventive maintenance procedures General maintenanceactivities follow aprescribed schedule that isdetailed in themaintenance trackingsystem. Nozzles and flowpatterns are checked daily;repairs are completed asneeded. Cleaning isperformed on a cyclematching machinedowntime.General maintenanceactivities follow aprescribed schedule that isdetailed in themaintenance trackingsystem. Nozzles and flowpatterns are checked daily;repairs are completed asneeded. Cleaning isperformed on a cyclematching machinedowntime.General maintenanceactivities follow aprescribed schedule that isdetailed in themaintenance trackingsystem. Nozzles and flowpatterns are checked daily;repairs are completed asneeded. Cleaning isperformed on a cyclematching machinedowntime.Problems experienced with control device within the last five years;how were problems solved?As reported in Title Vdeviation reports:equipment failure /repaired.As reported in Title Vdeviation reports:equipment failure /repaired.As reported in Title Vdeviation reports:equipment failure /repaired.Continuous monitoring method(s) used to monitor scrubberperformance, including parameters monitoredwater flow (gpm) &differential pressure.water flow (gpm) &differential pressure.water flow (gpm) &differential pressure.Plans to replace or upgrade scrubber None currently approvedor scheduled at this time.None currently approvedor scheduled at this time.None currently approvedor scheduled at this time.FORM C-2AIR POLLUTION CONTROLII. ScrubberFor each Scrubber:Process line(s) (identification name/number)Equipment/process(es) controlled. Include emission pointdesignations (e.g., E3, E4 from plot plan)Nature and frequency of preventive maintenance proceduresProblems experienced with control device within the last five years;how were problems solved?Continuous monitoring method(s) used to monitor scrubberperformance, including parameters monitoredPlans to replace or upgrade scrubberScrubber 4 Scrubber 5 Scrubber 6K5 J6 J6K5 Cooling (K5COOLINGand K5SCRUBBER002)(Stack 07-17)J6 Cooling (J6COOLINGand J6SCRUBBER001)(Stack 08-12)J6 Cooling (J6COOLINGand J6SCRUBBER002)(Stack 09-10)General maintenanceactivities follow aprescribed schedule that isdetailed in themaintenance trackingsystem. Nozzles and flowpatterns are checked daily;repairs are completed asneeded. Cleaning isperformed on a cyclematching machinedowntime.General maintenanceactivities follow aprescribed schedule that isdetailed in themaintenance trackingsystem. Nozzles and flowpatterns are checked daily;repairs are completed asneeded. Cleaning isperformed on a cyclematching machinedowntime.General maintenanceactivities follow aprescribed schedule that isdetailed in themaintenance trackingsystem. Nozzles and flowpatterns are checked daily;repairs are completed asneeded. Cleaning isperformed on a cyclematching machinedowntime.As reported in Title Vdeviation reports:equipment failure /repaired.As reported in Title Vdeviation reports:restricted water flow /repaired.As reported in Title Vdeviation reports:restricted water flow /repaired.water flow (gpm) &differential pressure.water flow (gpm) &differential pressure.water flow (gpm) &differential pressure.None currently approvedor scheduled at this time.None currently approvedor scheduled at this time.None currently approvedor scheduled at 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) J6 K5 70Equipment/process(es) controlled. Include emissionpoint designations (e.g., E3, E4 from plot plan)J5 Batch (J5 BATCH, CEJ5DC001) (stack 03-02)K5 Batch (K5 BATCH, CE-K5DC001) (stack 03-26)70 Batch (70 BATCH, CE-70DC001) (stack 31-73A)Latitude (decimal degrees, six decimal places)39.149602839.149682239.1497289Longitude (decimal degrees, six decimal places)-94.6143314-94.6139181-94.6151661Stack or vent height (units)61.67 ft.62.83 ft.10.08 ft.Stack or vent diameter (units)0.83 ft.0.83 ft.0.92 ft.Manufacturer and model Flex Kleen Farr Flex KleenDate of original installation 2006 2008 2007Number of compartments 1 1 1Number of bags per compartment 36 6 49Filter material and coatings applied Polyestermedia No data available. Polyester mediaFabric weight (oz/yd2)8 No data available. 8 oz/yd2Filter surface area (ft2) 720 ft2No data available.980 ft2Gas flow rate to filter (acfm @°F)No data available. No data available. No data available.Inlet gas temperature (°F)Ambient Ambient AmbientOutlet gas temperature (°F)Ambient Ambient AmbientInlet grain loading (gr/dscf) No data available. No data available. No data available.Outlet grain loading (gr/dscf) <0.02 gr/dscf <0.02 gr/dscf <0.02 gr/dscfAverage stack opacity (%) <20% <20% <20%Overall pressure drop (in. H2O gauge) No data available. No data available. No dataavailable.Method and frequency of bag cleaning No data available. No data available. No data available.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 4 Fabric Filter 5 Fabric Filter 6J6, K5 and 70 J6, K5 and 70 J6, K5 and 70Raw Material Storage Bin #1(BATCHHOUSE1, CEDCRMBIN1) (stack B-01)Raw Material Storage Bin#2A (BATCHHOUSE2A, CEDCRMBIN2A) (stack B-02)Raw Material Storage Bin#2B (BATCHHOUSE2B, CEDCRMBIN2B) (stack B-03)39.149173139.149183939.149225-94.6135106-94.6135103-94.613509244.5 ft.44.5 ft.44.5 ft.0.61 ft.0.61 ft.0.61 ft.Manufacturer not known.Model No. 96AVS16, Style#2Manufacturer not known.Model No. 96AVS16, Style#2Manufacturer not known.Model No. 96AVS16, Style#22008 2008 20081 1 116 16 16Polypro Polypro Polypro16 oz/yd216 oz/yd216 oz/yd276.25 ft276.25 ft276.25 ft2No data available. No data available. No data available.Ambient Ambient AmbientAmbient Ambient AmbientNo data available. No data available. No data available.<0.02 gr/dscf <0.02 gr/dscf <0.02 gr/dscf<20% <20% <20%No data available. No data available. No data available.No data available. No data available. No data available.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 7 Fabric Filter 8 Fabric Filter 9J6, K5 and 70 J6, K5 and 70 J6, K5 and 70Raw Material Storage Bin #3(BATCHHOUSE3, CEDCRMBIN3) (stack B-04)Raw Material Storage Bin #4(BATCHHOUSE4, CEDCRMBIN4) (stack B-05)Raw Material Storage Bin#5A (BATCHHOUSE5A, CEDCRMBIN5A) (stack B-06)39.149236139.149288339.1493322-94.6135089-94.6135072-94.613506144.5 ft.44.5 ft.44.5 ft.0.61 ft.0.61 ft.0.61 ft.Manufacturer not known.Model No. 96AVS16, Style#2Manufacturer not known.Model No. 96AVS16, Style#2Manufacturer not known.Model No. 96AVS16, Style#22008 20208 20081 1 116 16 16Polypro Polypro Polypro16 oz/yd216 oz/yd216 oz/yd276.25 ft276.25 ft276.25 ft2No data available. No data available. No data available.Ambient Ambient AmbientAmbient Ambient AmbientNo data available. No data available. No data available.<0.02 gr/dscf <0.02 gr/dscf <0.02 gr/dscf<20% <20% <20%No data available. No data available. No data available.No data available. No data available. No data available.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 10 Fabric Filter 11 Fabric Filter 12J6, K5 and 70 J6, K5 and 70 J6, K5 and 70Raw Material Storage Bin#5B (BATCHHOUSE5B, CEDCRMBIN5B) (stack B-07)Raw Material Storage Bin #6(BATCHHOUSE6, CEDCRMBIN6) (stack B-08)Raw Material Storage Bin#7A (BATCHHOUSE7A, CEDCRMBIN7A) (stack B-09)39.149340339.149436439.1494447-94.6135058-94.6135031-94.613503144.5 ft.44.5 ft.44.5 ft.0.61 ft.0.61 ft.0.61 ft.Manufacturer not known.Model No. 96AVS16, Style#2Manufacturer not known.Model No. 96AVS16, Style#2Manufacturer not known.Model No. 96AVS16, Style#22008 2008 20081 1 116 16 16Polypro Polypro Polypro16 oz/yd216 oz/yd216 oz/yd276.25 ft276.25 ft276.25 ft2No data available. No data available. No data available.Ambient Ambient AmbientAmbient Ambient AmbientNo data available. No data available. No data available.<0.02 gr/dscf <0.02 gr/dscf <0.02 gr/dscf<20% <20% <20%No data available. No data available. No data available.No data available. No data available. No data available.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 13 Fabric Filter 14 Fabric Filter 15J6, K5 and 70 J6, K5 and 70 J6, K5 and 70Raw Material Storage Bin#7B (BATCHHOUSE7B)(stack B-10)Raw Material Storage Bin #8(BATCHHOUSE8) (stack B11)Raw Material Storage Bin #9(BATCHHOUSE9, CEDCRMBIN9) (stack B-13)39.1494886 (stack B-10)39.1494969 (stack B-11)39.1492186 (stack B-13)-94.6135017 (stack B-10)-94.6135014 (stack B-11)-94.6134328 (stack B-13)44.5 ft.44.5 ft.44.5 ft.0.61 ft.0.61 ft.0.61 ft.Manufacturer not known.Model No. 96AVS16, Style#2Manufacturer not known.Model No. 96AVS16, Style#2Manufacturer not known.Model No. 96AVS16, Style#220008 2008 20081 1 116 16 16Polypro Polypro Polypro16 oz/yd216 oz/yd216 oz/yd276.25 ft276.25 ft276.25 ft2No data available. No data available. No data available.Ambient Ambient AmbientAmbient Ambient AmbientNo data available. No data available. No data available.<0.02 gr/dscf <0.02 gr/dscf <0.02 gr/dscf<20% <20% <20%No data available. No data available. No data available.No data available. No data available. No data available.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 16 Fabric Filter 17 Fabric Filter 18J6, K5 and 70 J6, K5 and 70 J6, K5 and 70Raw Material WestUnloading(BATCHHOUSEUL, CEDCRUNLOAD) (stack B-20)Raw Material East Unloading(stack B-24)Raw Material Mixing(BATCHHOUSEMIX, CEDCBHMIXER) (stack B-26)39.1495447 (stack B-20)39.149239439.1492711-94.6135 (stack B-20)-94.6133892-94.613521933.5 ft.0.08 ft.9.50 ft.1 ft.12.92 ft.1.0 ft.Tech Air - SZ85-10-1334(Serial No. 11-93-9248)Flex Kleen 43/54-PSBL121(IIIG)No data available.2008 2008 20081 1 185 No data available. 40Polyester No data available. No data available.16 oz/yd2No data available.16 oz/yd2405 ft25,203 ft2190 ft2No data available. No data available. No data available.Ambient Ambient AmbientAmbient Ambient AmbientNo data available. No data available. No data available.<0.02 gr/dscf <0.02 gr/dscf <0.02 gr/dscf<20% <20% <20%No data available. 20" No data available.No data available. Manual. No frequency. No data available.None provided. None provided. 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) J6 K5 70Equipment/process(es) controlled. Include emissionpoint designations (e.g., E3, E4 from plot plan)J5 Batch (J5 BATCH, CEJ5DC001) (stack 03-02)K5 Batch (K5 BATCH, CE-K5DC001) (stack 03-26)70 Batch (70 BATCH, CE-70DC001) (stack 31-73A)Quantity of solid waste collected (lbs/yr) N/A(Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)Quantity of solid waste recycled (lbs/yr) N/A(Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)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 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.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?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 N/APlans to replace or upgrade fabric filter Nonecurrently approved orscheduled at this time.None currently approved orscheduled at this time.None currently approved orscheduled at 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 4 Fabric Filter 5 Fabric Filter 6J6, K5 and 70 J6, K5 and 70 J6, K5 and 70Raw Material Storage Bin #1(BATCHHOUSE1, CEDCRMBIN1) (stack B-01)Raw Material Storage Bin#2A (BATCHHOUSE2A, CEDCRMBIN2A) (stack B-02)Raw Material Storage Bin#2B (BATCHHOUSE2B, CEDCRMBIN2B) (stack B-03)N/A (Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)0 lbs 0 lbs 0 lbsN/A N/A N/AGeneral 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.General maintenance repairsas needed. Visualinspections and differentialpressure checks areperformed routinely. Bag orcartridge replacement isperformed as needed.None reported in Title Vdeviation reports.None reported in Title Vdeviation reports.None reported in Title Vdeviation reports.N/A N/A N/ANone currently approved orscheduled at this time.None currently approved orscheduled at this time.None currently approved orscheduled at 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 7 Fabric Filter 8 Fabric Filter 9J6, K5 and 70 J6, K5 and 70 J6, K5 and 70Raw Material Storage Bin #3(BATCHHOUSE3, CEDCRMBIN3) (stack B-04)Raw Material Storage Bin #4(BATCHHOUSE4, CEDCRMBIN4) (stack B-05)Raw Material Storage Bin#5A (BATCHHOUSE5A, CEDCRMBIN5A) (stack B-06)N/A (Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)0 lbs 0 lbs 0 lbsN/A N/A N/AGeneral 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.General maintenance repairsas needed. Visualinspections and differentialpressure checks areperformed routinely. Bag orcartridge replacement isperformed as needed.None reported in Title Vdeviation reports.None reported in Title Vdeviation reports.None reported in Title Vdeviation reports.N/A N/A N/ANone currently approved orscheduled at this time.None currently approved orscheduled at this time.None currently approved orscheduled at 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 10 Fabric Filter 11 Fabric Filter 12J6, K5 and 70 J6, K5 and 70 J6, K5 and 70Raw Material Storage Bin#5B (BATCHHOUSE5B, CEDCRMBIN5B) (stack B-07)Raw Material Storage Bin #6(BATCHHOUSE6, CEDCRMBIN6) (stack B-08)Raw Material Storage Bin#7A (BATCHHOUSE7A, CEDCRMBIN7A) (stack B-09)N/A (Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)0 lbs 0 lbs 0 lbsN/A N/A N/AGeneral 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.General maintenance repairsas needed. Visualinspections and differentialpressure checks areperformed routinely. Bag orcartridge replacement isperformed as needed.None reported in Title Vdeviation reports.None reported in Title Vdeviation reports.None reported in Title Vdeviation reports.N/A N/A N/ANone currently approved orscheduled at this time.None currently approved orscheduled at this time.None currently approved orscheduled at 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 13 Fabric Filter 14 Fabric Filter 15J6, K5 and 70 J6, K5 and 70 J6, K5 and 70Raw Material Storage Bin#7B (BATCHHOUSE7B)(stack B-10)Raw Material Storage Bin #8(BATCHHOUSE8) (stack B11)Raw Material Storage Bin #9(BATCHHOUSE9, CEDCRMBIN9) (stack B-13)N/A (Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)0 lbs 0 lbs 0 lbsN/A N/A N/AGeneral 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.General maintenance repairsas needed. Visualinspections and differentialpressure checks areperformed routinely. Bag orcartridge replacement isperformed as needed.None reported in Title Vdeviation reports.None reported in Title Vdeviation reports.None reported in Title Vdeviation reports.N/A N/A N/ANone currently approved orscheduled at this time.None currently approved orscheduled at this time.None currently approved orscheduled at 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 16 Fabric Filter 17 Fabric Filter 18J6, K5 and 70 J6, K5 and 70 J6, K5 and 70Raw Material WestUnloading(BATCHHOUSEUL, CEDCRUNLOAD) (stack B-20)Raw Material East Unloading(stack B-24)Raw Material Mixing(BATCHHOUSEMIX, CEDCBHMIXER) (stack B-26)N/A (Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)N/A (Closed system returnscollected dust to process.)0 lbs 0 lbs 0 lbsN/A N/A N/AGeneral 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.General maintenance repairsas needed. Visualinspections and differentialpressure checks areperformed routinely. Bag orcartridge replacement isperformed as needed.None reported in Title Vdeviation reports.None reported in Title Vdeviation reports.None reported in Title Vdeviation reports.N/A N/A N/ANone currently approved orscheduled at this time.None currently approved orscheduled at this time.None currently approved orscheduled at this time.FORM C-5AIR POLLUTION CONTROLNot applicable to this facility.V. Thermal IncineratorFor 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/AContinuous monitoring method(s) used to monitorincinerator performance, including parameters monitoredN/AFORM C-5AIR POLLUTION CONTROLNot applicable to this facility.V. Thermal IncineratorFor 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/APlans to replace or upgrade thermal incinerator N/AFORM C-6AIR POLLUTION CONTROLVI. High Velocity Air Filter (HVAF)For each HVAF:HVAF 1 HVAF 2 HVAF 3Process line(s) (identification name/number) 70 70 K5Equipment/process(es) controlled. Include emissionpoint designations (e.g., E3, E4 from plot plan)70 Cooling (North SmokeStripper) (Stack SV-18-11)70 Cooling (South SmokeStripper) (Stack SV-18-11)K5 Cooling (North SmokeStripper) (Stack SV-08-10)Latitude (decimal degrees, six decimal places)39.149062539.149062539.1487397Longitude (decimal degrees, six decimal places)-94.6151425-94.6151425-94.6140753Stack or vent height (units)37.58 ft.37.58 ft.42 ft.Stack or vent diameter (units)1.67 ft.1.67 ft.1 ft.Manufacturer and model OC Proprietary Design OCProprietary Design OC Proprietary DesignDate of original installation 1985 1985 UnknownInlet gas flow rate (acfm @°F)5,018 acfm @ 122 °F 5,018 acfm @ 122 °F 6,349 acfm @139 °FInlet gas temperature (°F)No data available. No data available. No data available.Outlet gas temperature (°F)100-150 °F 100-150 °F 100-150 °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%Water spray pressure (sdig), if applicable Nodata available. No data available. No data available.Water spray rate (gpm), if applicable 20 - 60gpm 20 - 60 gpm 20 - 60 gpmFilter face velocity (acfm/ft2)No data available. No data available. No data available.Maximum pressure drop across mat (in. H2O gauge) No data available. No data available. No dataavailable.Vendor guarantee on HVAF efficiency (attach copy) N/A N/A N/AMethod and frequency of filter mad advancement Filters pads are replaced onceper shift.Filters pads are replaced onceper shift.Filters pads are replaced onceper shift.Amount of wastewater generated (gpd) 0 gpd (infrequent discharges) 0 gpd (infrequent discharges) 0gpd (infrequent discharges)Amount of wastewater recycled (gpd) 100% 100% 100%Amount of wastewater disposed of (gpd) 0 gpd (infrequent discharges) 0 gpd (infrequent discharges)0 gpd (infrequent discharges)Method of wastewater disposal N/A N/A N/AFORM C-6AIR POLLUTION CONTROLVI. High Velocity Air Filter (HVAF)For each HVAF: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 installationInlet gas flow rate (acfm @°F)Inlet gas temperature (°F)Outlet gas temperature (°F)Inlet grain loading (gr/dscf)Outlet grain loading (gr/dscf)Average stack opacity (%)Water spray pressure (sdig), if applicableWater spray rate (gpm), if applicableFilter face velocity (acfm/ft2)Maximum pressure drop across mat (in. H2O gauge)Vendor guarantee on HVAF efficiency (attach copy)Method and frequency of filter mad advancementAmount of wastewater generated (gpd)Amount of wastewater recycled (gpd)Amount of wastewater disposed of (gpd)Method of wastewater disposalHVAF 4 HVAF 5 HVAF 6K5 J6 J6K5 Cooling (South SmokeStripper) (Stack SV-08-10)J6 Cooling (North SmokeStripper) (Stack SV-10-07)J6 Cooling (South SmokeStripper) (Stack SV-10-07)39.148739739.149118639.1491186-94.6140753-94.6142931-94.614293142 ft.42.50 ft.42.50 ft.1 ft.1.67 ft.1.67 ft.OC Proprietary Design OC Proprietary Design OC Proprietary DesignUnknown Unknown Unknown6,349 acfm @ 139 °F 7,898 acfm @ 121 °F 7,898 acfm @121 °FNo data available. No data available. No data available.100-150 °F 100-120 °F 100-120 °FNo data available. No data available. No data available.No data available. No data available. No data available.<20% <20% <20%No data available. No data available. No data available.20 - 60 gpm 20 - 60 gpm 20 - 60 gpmNo data available. No data available. No data available.No data available. No data available. No data available.N/A N/A N/AFilters pads are replaced onceper shift.Filters pads are replaced onceper shift.Filters pads are replaced onceper shift.0 gpd (infrequent discharges) 0 gpd (infrequent discharges) 0 gpd (infrequent discharges)100% 100% 100%0 gpd (infrequent discharges) 0 gpd (infrequent discharges) 0 gpd (infrequent discharges)N/A N/A N/AFORM C-6AIR POLLUTION CONTROLVI. High Velocity Air Filter (HVAF)For each HVAF: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 installationInlet gas flow rate (acfm @°F)Inlet gas temperature (°F)Outlet gas temperature (°F)Inlet grain loading (gr/dscf)Outlet grain loading (gr/dscf)Average stack opacity (%)Water spray pressure (sdig), if applicableWater spray rate (gpm), if applicableFilter face velocity (acfm/ft2)Maximum pressure drop across mat (in. H2O gauge)Vendor guarantee on HVAF efficiency (attach copy)Method and frequency of filter mad advancementAmount of wastewater generated (gpd)Amount of wastewater recycled (gpd)Amount of wastewater disposed of (gpd)Method of wastewater disposalHVAF 7 HVAF 8 HVAF 970 70 7070 Curing (Oven Charge -North HPAF) (Stack SV-18-06)70 Curing (Oven Charge -South HPAF) (Stack SV-18-06)70 Curing (Oven DischargeNorth HPAF) (Stack SV-17-06)39.149417239.149417239.1491572-94.6151708-94.6151708-94.615024242.27 ft.42.27 ft.37.84 ft.2.50 ft.2.50 ft.2 ft.OC Proprietary Design OC Proprietary Design OC Proprietary Design1986 1984 Unknown9,694 acfm @ 125 °F 9,694 acfm @ 125 °F 9,327 acfm @132 °FNo data available. No data available. No data available.120-130 °F 120-130 °F 100-150 °FNo data available. No data available. No data available.No data available. No data available. No data available.<20% <20% <20%No data available. No data available. No data available.32.5 - 65.5 gpm 32.5 - 65.5 gpm 32.5 - 65.5 gpmNo data available. No data available. No data available.No data available. No data available. No data available.N/A N/A N/AFilters pads are replaced onceper shift.Filters pads are replaced onceper shift.Filters pads are replaced onceper shift.0 gpd (infrequent discharges) 0 gpd (infrequent discharges) 0 gpd (infrequent discharges)100% 100% 100%0 gpd (infrequent discharges) 0 gpd (infrequent discharges) 0 gpd (infrequent discharges)N/A N/A N/AFORM C-6AIR POLLUTION CONTROLVI. High Velocity Air Filter (HVAF)For each HVAF: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 installationInlet gas flow rate (acfm @°F)Inlet gas temperature (°F)Outlet gas temperature (°F)Inlet grain loading (gr/dscf)Outlet grain loading (gr/dscf)Average stack opacity (%)Water spray pressure (sdig), if applicableWater spray rate (gpm), if applicableFilter face velocity (acfm/ft2)Maximum pressure drop across mat (in. H2O gauge)Vendor guarantee on HVAF efficiency (attach copy)Method and frequency of filter mad advancementAmount of wastewater generated (gpd)Amount of wastewater recycled (gpd)Amount of wastewater disposed of (gpd)Method of wastewater disposalHVAF 10 HVAF 11 HVAF 1270 K5 K570 Curing (Oven DischargeSouth HPAF) (Stack SV-17-06)K5 Curing (Oven ChargeNorth HPAF) (Stack SV-08-15)K5 Curing (Oven ChargeSouth HPAF) (Stack SV-08-15)39.149157239.149096139.1490961-94.6150242-94.6140361-94.614036137.84 ft.45 ft.45 ft.2 ft.2.5 ft.2.5 ft.OC Proprietary Design OC Proprietary Design OC Proprietary DesignUnknown 1985 19859,327 acfm @ 132 °F 13,339 acfm @ 147 °F 13,339 acfm@ 147 °FNo data available. No data available. No data available.100-150 °F 120-130 °F 120-130 °FNo data available. No data available. No data available.No data available. No data available. No data available.<20% <20% <20%No data available. No data available. No data available.32.5 - 65.5 gpm 32.5 - 65.5 gpm 32.5 - 65.5 gpmNo data available. No data available. No data available.No data available. No data available. No data available.N/A N/A N/AFilters pads are replaced onceper shift.Filters pads are replaced onceper shift.Filters pads are replaced onceper shift.0 gpd (infrequent discharges) 0 gpd (infrequent discharges) 0 gpd (infrequent discharges)100% 100% 100%0 gpd (infrequent discharges) 0 gpd (infrequent discharges) 0 gpd (infrequent discharges)N/A N/A N/AFORM C-6AIR POLLUTION CONTROLVI. High Velocity Air Filter (HVAF)For each HVAF: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 installationInlet gas flow rate (acfm @°F)Inlet gas temperature (°F)Outlet gas temperature (°F)Inlet grain loading (gr/dscf)Outlet grain loading (gr/dscf)Average stack opacity (%)Water spray pressure (sdig), if applicableWater spray rate (gpm), if applicableFilter face velocity (acfm/ft2)Maximum pressure drop across mat (in. H2O gauge)Vendor guarantee on HVAF efficiency (attach copy)Method and frequency of filter mad advancementAmount of wastewater generated (gpd)Amount of wastewater recycled (gpd)Amount of wastewater disposed of (gpd)Method of wastewater disposalHVAF 13 HVAF 14 HVAF 15K5 K5 J6K5 Curing (Oven DischargeNorth HPAF) (Stack SV-08-11)K5 Curing (Oven DischargeSouth HPAF) (Stack SV-08-11)J6 Curing (Oven Charge NorthHPAF) (Stack SV-10-06)39.148802539.148802539.149295-94.6140422-94.6140422-94.614306140.5 ft.40.5 ft.37.75 ft.2.5 ft.2.5 ft.1.83 ft.OC Proprietary Design OC Proprietary Design OC Proprietary Design1987 1987 Unknown6,677 acfm @ 141 °F 6,677 acfm @ 141 °F 10,033 acfm @148 °FNo data available. No data available. No data available.100-150 °F 100-150 °F 120-130 °FNo data available. No data available. No data available.No data available. No data available. No data available.<20% <20% <20%No data available. No data available. No data available.32.5 - 65.5 gpm 32.5 - 65.5 gpm 32.5 - 65.5 gpmNo data available. No data available. No data available.No data available. No data available. No data available.N/A N/A N/AFilters pads are replaced onceper shift.Filters pads are replaced onceper shift.Filters pads are replaced onceper shift.0 gpd (infrequent discharges) 0 gpd (infrequent discharges) 0 gpd (infrequent discharges)100% 100% 100%0 gpd (infrequent discharges) 0 gpd (infrequent discharges) 0 gpd (infrequent discharges)N/A N/A N/AFORM C-6AIR POLLUTION CONTROLVI. High Velocity Air Filter (HVAF)For each HVAF: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 installationInlet gas flow rate (acfm @°F)Inlet gas temperature (°F)Outlet gas temperature (°F)Inlet grain loading (gr/dscf)Outlet grain loading (gr/dscf)Average stack opacity (%)Water spray pressure (sdig), if applicableWater spray rate (gpm), if applicableFilter face velocity (acfm/ft2)Maximum pressure drop across mat (in. H2O gauge)Vendor guarantee on HVAF efficiency (attach copy)Method and frequency of filter mad advancementAmount of wastewater generated (gpd)Amount of wastewater recycled (gpd)Amount of wastewater disposed of (gpd)Method of wastewater disposalHVAF 16 HVAF 17 HVAF 18J6 J6 J6J6 Curing (Oven ChargeSouth HPAF) (Stack SV-10-06)J6 Curing (Oven DischargeNorth HPAF) (Stack SV-10-11)J6 Curing (Oven DischargeSouth HPAF) (Stack SV-10-11)39.14929539.1491739.14917-94.6143061-94.6143386-94.614338637.75 ft.35.58 ft.35.58 ft.1.83 ft.1.83 ft.1.83 ft.OC Proprietary Design OC Proprietary Design OC Proprietary DesignUnknown Unknown Unknown10,033 acfm @ 148 °F 11,165 acfm @ 133 °F 11,165 acfm@ 133 °FNo data available. No data available. No data available.120-130 °F 100-150 °F 100-150 °FNo data available. No data available. No data available.No data available. No data available. No data available.<20% <20% <20%No data available. No data available. No data available.32.5 - 65.5 gpm 32.5 - 65.5 gpm 32.5 - 65.5 gpmNo data available. No data available. No data available.No data available. No data available. No data available.N/A N/A N/AFilters pads are replaced onceper shift.Filters pads are replaced onceper shift.Filters pads are replaced onceper shift.0 gpd (infrequent discharges) 0 gpd (infrequent discharges) 0 gpd (infrequent discharges)100% 100% 100%0 gpd (infrequent discharges) 0 gpd (infrequent discharges) 0 gpd (infrequent discharges)N/A N/A N/AFORM C-6AIR POLLUTION CONTROLVI. High Velocity Air Filter (HVAF)For each HVAF:HVAF 1 HVAF 2 HVAF 3Process line(s) (identification name/number) 70 70 K5Equipment/process(es) controlled. Include emissionpoint designations (e.g., E3, E4 from plot plan)70 Cooling (North SmokeStripper) (Stack SV-18-11)70 Cooling (South SmokeStripper) (Stack SV-18-11)K5 Cooling (North SmokeStripper) (Stack SV-08-10)Quantity of solid waste collected (lbs/yr) 39,000 lbs 39,000 lbs 39,000 lbsQuantity of solid waste recycled (lbs/yr) 0 lbs/yr 0 lbs/yr 0 lbs/yrQuantity of solid waste disposed of (lbs/yr) 39,000 lbs 39,000 lbs 39,000 lbsMethod 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.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.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?As reported in Title V deviationreports: electrical malfunction /repaired; equipment failure /repaired; and opacity /repaired and reset.As reported in Title V deviationreports: electrical malfunction /repaired; equipment failure /repaired; and opacity /repaired and reset.As reported in Title V deviationreports: electrical malfunction /repaired; and equipmentfailure / repaired.Continuous monitoring method(s) used to monitorHVAF performance, including parameters monitoredN/A N/A N/APlans 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-6AIR POLLUTION CONTROLVI. High Velocity Air Filter (HVAF)For each HVAF: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 monitorHVAF performance, including parameters monitoredPlans to replace or upgrade HVAFHVAF 4 HVAF 5 HVAF 6K5 J6 J6K5 Cooling (South SmokeStripper) (Stack SV-08-10)J6 Cooling (North SmokeStripper) (Stack SV-10-07)J6 Cooling (South SmokeStripper) (Stack SV-10-07)39,000 lbs 39,000 lbs 39,000 lbs0 lbs/yr 0 lbs/yr 0 lbs/yr39,000 lbs 39,000 lbs 39,000 lbsLocal Solid Waste Landfill Local Solid Waste Landfill Local Solid Waste LandfillGeneral 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.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.Nozzles and flow patterns arechecked daily; repairs arecompleted as needed.Cleaning is performed on acycle matching machinedowntime.As reported in Title V deviationreports: electrical malfunction /repaired; and equipmentfailure / repaired.None reported in Title Vdeviation reports.None reported in Title Vdeviation reports.N/A N/A N/ANone 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: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 monitorHVAF performance, including parameters monitoredPlans to replace or upgrade HVAFHVAF 7 HVAF 8 HVAF 970 70 7070 Curing (Oven Charge -North HPAF) (Stack SV-18-06)70 Curing (Oven Charge -South HPAF) (Stack SV-18-06)70 Curing (Oven DischargeNorth HPAF) (Stack SV-17-06)39,000 lbs 39,000 lbs 39,000 lbs0 lbs/yr 0 lbs/yr 0 lbs/yr39,000 lbs 39,000 lbs 39,000 lbsLocal Solid Waste Landfill Local Solid Waste Landfill Local Solid Waste LandfillGeneral 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.Cleaning is performed on acycle matched to machinedowntime.General maintenance activitiesfollow a prescribed schedulethat is detailed in themaintenance tracking system.Cleaning is performed on acycle matched to machinedowntime.As reported in Title V deviationreports: electrical malfunction /repaired; equipment failure /repaired; and opacity /repaired and reset.As reported in Title V deviationreports: electrical malfunction /repaired; equipment failure /repaired; and opacity /repaired and reset.As reported in Title V deviationreports: electrical malfunction /repaired; equipment failure /repaired; and opacity /repaired and reset.Water Flow Water Flow Water FlowNone 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: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 monitorHVAF performance, including parameters monitoredPlans to replace or upgrade HVAFHVAF 10 HVAF 11 HVAF 1270 K5 K570 Curing (Oven DischargeSouth HPAF) (Stack SV-17-06)K5 Curing (Oven ChargeNorth HPAF) (Stack SV-08-15)K5 Curing (Oven ChargeSouth HPAF) (Stack SV-08-15)39,000 lbs 39,000 lbs 39,000 lbs0 lbs/yr 0 lbs/yr 0 lbs/yr39,000 lbs 39,000 lbs 39,000 lbsLocal Solid Waste Landfill Local Solid Waste Landfill Local Solid Waste LandfillGeneral 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.Cleaning is performed on acycle matched to machinedowntime.General maintenance activitiesfollow a prescribed schedulethat is detailed in themaintenance tracking system.Cleaning is performed on acycle matched to machinedowntime.As reported in Title V deviationreports: electrical malfunction /repaired; equipment failure /repaired; and opacity /repaired and reset.As reported in Title V deviationreports: electrical malfunction /repaired; and equipmentfailure / repaired.As reported in Title V deviationreports: electrical malfunction /repaired; and equipmentfailure / repaired.Water Flow Water Flow Water FlowNone 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: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 monitorHVAF performance, including parameters monitoredPlans to replace or upgrade HVAFHVAF 13 HVAF 14 HVAF 15K5 K5 J6K5 Curing (Oven DischargeNorth HPAF) (Stack SV-08-11)K5 Curing (Oven DischargeSouth HPAF) (Stack SV-08-11)J6 Curing (Oven Charge NorthHPAF) (Stack SV-10-06)39,000 lbs 39,000 lbs 39,000 lbs0 lbs/yr 0 lbs/yr 0 lbs/yr39,000 lbs 39,000 lbs 39,000 lbsLocal Solid Waste Landfill Local Solid Waste Landfill Local Solid Waste LandfillGeneral 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.Cleaning is performed on acycle matched to machinedowntime.General maintenance activitiesfollow a prescribed schedulethat is detailed in themaintenance tracking system.Cleaning is performed on acycle matched to machinedowntime.As reported in Title V deviationreports: electrical malfunction /repaired; and equipmentfailure / repaired.As reported in Title V deviationreports: electrical malfunction /repaired; and equipmentfailure / repaired.None reported in Title Vdeviation reports.Water Flow Water Flow Water FlowNone 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: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 monitorHVAF performance, including parameters monitoredPlans to replace or upgrade HVAFHVAF 16 HVAF 17 HVAF 18J6 J6 J6J6 Curing (Oven ChargeSouth HPAF) (Stack SV-10-06)J6 Curing (Oven DischargeNorth HPAF) (Stack SV-10-11)J6 Curing (Oven DischargeSouth HPAF) (Stack SV-10-11)39,000 lbs 39,000 lbs 39,000 lbs0 lbs/yr 0 lbs/yr 0 lbs/yr39,000 lbs 39,000 lbs 39,000 lbsLocal Solid Waste Landfill Local Solid Waste Landfill Local Solid Waste LandfillGeneral 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.Cleaning is performed on acycle matched to machinedowntime.General maintenance activitiesfollow a prescribed schedulethat is detailed in themaintenance tracking system.Cleaning is performed on acycle matched to machinedowntime.None reported in Title Vdeviation reports.None reported in Title Vdeviation reports.None reported in Title Vdeviation reports.Water Flow Water Flow Water FlowNone 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 Vents(various)Latitude (decimal degrees, six decimal places)39.148578Longitude (decimal degrees, six decimal places)-94.614942Stack or vent height (units)Roof ht.Stack or vent diameter (units)VariousFor 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): Other APCD 1 Other APCD 2Process line(s) (identification name/number) 70 K5Equipment/process(es) controlled. Include emission pointdesignations (e.g., E3, E4 from plot plan)70 Forming (70FORMING)K5 Forming (K5FORMINGNand K5FORMINGS)Latitude (decimal degrees, six decimal places) 39.1493044 (stack 01-07),39.1500183 (stack 01-08),39.1494297 (stack 01-09)and 39.1494853 (stack 01-10)39.1492742 (stack 04-11),39.1493311 (stack 04-12),39.1494586 (stack 04-14)and 39.1494919 (stack 04-16)Longitude (decimal degrees, six decimal places)-94.6147317 (stack 01-07), -94.6147239 (stack 01-08), -94.6148525 (stack 01-09)and -94.6149111 (stack 01-10)-94.6138611 (stack 04-11), -94.6141175 (stack 04-12), -94.6141147 (stack 04-14)and -94.6141353 (stack 04-16)Stack or vent height (units)93.40 ft. (stack 01-07),100.75 ft. (stack 01-08),99.40 ft. (stack 01-09) and93.40 ft. (stack 01-10)79.18 ft. (stack 04-11),100.75 ft. (stack 04-12),92.35 ft. (stack 04-14) and88.98 ft. (stack 04-16)Stack or vent diameter (units)4.33 ft. (stack 01-07), 4.58ft. (stack 01-08), 4.00 ft.(stack 01-09) and 4.33 ft.(stack 01-10)3.42 ft. (stack 04-11), 4.58ft. (stack 04-12), 3.75 ft.(stack 04-14) and 3.422 ft.(stack 04-16)DescriptionDrop-Out Boxes withCyclonic SeparatorsDrop-Out Boxes withCyclonic SeparatorsFORM C-9AIR POLLUTION CONTROLIX. OtherFor each Other Air Pollution Control Device (APCD):Process line(s) (identification name/number)Equipment/process(es) controlled. Include emission pointdesignations (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)DescriptionOther APCD 37070 Furnace (70FURNACE)39.1496769 (stack 01-03)and 39.1495919 (stack 01-04)-94.6150889 (stack 01-03)and -94.6150906 (stack 01-04)67.11 ft (each)4.00 ft. (each)Batch WettingFORM 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 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.The 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.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.