R13 PERMIT APPLICATIONdep.wv.gov/daq/Documents/October 2016 Applications/003-00154_APPL_13... · P&G – Tabler Station | R13 Permit Trinity Consultants 3 1. INTRODUCTION 1.1. FACILITY
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Environmental solutions delivered uncommonly well
R13 PERMIT APPLICATION Procter and Gamble
Tabler Station, West Virginia
PreparedBy:
TRINITYCONSULTANTS15ESalemAve.
Suite201Roanoke,VA24011
(540)342‐5945
Submitted:April2016Revised:October2016
Project141801.0078
P&G – Tabler Station | R13 Permit Trinity Consultants 1
TABLE OF CONTENTS
1. INTRODUCTION 3
1.1.FacilityandProjectDescription 3
1.2.R‐13ApplicationOrganization 3
2. SAMPLE EMISSION SOURCE CALCULATIONS 4
2.1.SurfactantManufacturing 4
2.1.1.ProcessDescription 4
2.1.2.EmissionsCalculations 5
2.2.LiquidSoapMakingAandB 6
2.2.1.ProcessDescription 6
2.2.2.EmissionsCalculations 7
2.3.DryConsumerLaundryandCleaningProductsA 7
2.3.1.ProcessDescription 7
2.3.2.EmissionsCalculations 8
2.4.Utilities 10
2.4.1.ProcessDescription 10
2.4.2.EmissionsCalculations 11
2.5.PlasticsMolding 11
2.5.1.ProcessDescription 11
2.5.2.EmissionsCalculationsforPlasticsMolding 12
2.6.PlasticsMoldingUtilities 12
2.6.1.ProcessDescription 12
2.6.2.EmissionsCalculations 13
2.7.SourcesofMinorSignificance 13
3. R13 APPLICATION FORM 14
ATTACHMENT A: CURRENT BUSINESS CERTIFICATE
ATTACHMENT B: MAP
ATTACHMENT C: INSTALLATION AND START UP SCHEDULE
ATTACHMENT D: REGULATORY DISCUSSION
ATTACHMENT E: PLOT PLAN
ATTACHMENT F: DETAILED PROCESS FLOW DIAGRAM
ATTACHMENT G: PROCESS DESCRIPTION
ATTACHMENT H: MATERIAL SAFETY DATA SHEETS
ATTACHMENT I: EMISSION UNITS TABLE
ATTACHMENT J: EMISSION POINTS DATA SUMMARY SHEET
ATTACHMENT K: FUGITIVE EMISSIONS DATA SUMMARY SHEET
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ATTACHMENT L: EMISSIONS UNIT DATA SHEETS
ATTACHMENT M: AIR POLLUTION CONTROL DEVICE SHEET
ATTACHMENT N: SUPPORTING EMISSION CALCULATIONS
ATTACHMENT O: MONITORING/RECORDKEEPING/REPORTING/TESTING PLANS
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1. INTRODUCTION
1.1. FACILITY AND PROJECT DESCRIPTION
ProcterandGamble(P&G)issubmittingthisRule‐13(R‐13)permitapplicationtotheWestVirginiaDepartmentofEnvironmentalProtection(DEP)fortheproposedconstructionofagreenfieldfacilitytobelocatedinBerkleyCounty,WestVirginiaintheunincorporatedcommunityofTablerStation(TablerStationfacility).TheTablerStationfacilitywillproduceliquidsoapanddryconsumerlaundryandcleaningproducts,includingdryerappliedfabricsoftener,shampoo,andbodywash.Thefacilitywillproducesurfactantpasteandrawmaterialswhichwillbeusedinliquidsoapmakingprocesses.Thefacilitywillhaveutilitiestosupporttheheating,cooling,ventilation,andsteamneedsofthemanufacturingprocesses.Thefacilitywillincorporatethirdpartysupplierswhowillprovideaplasticsmoldingprocessforthemanufactureofbottles,caps,andotherformedplasticparts.Theequipmentandoperationsatthefacilitywillbeinstalledandstartedupinmultiplephases.Thebusinessoperationscontainedinthispermitapplicationarethoseexpectedtobeinstalledinthefirstphaseoftheproject.Additionalphasesarestillindetaileddesignandwillbepermittedatalaterdate.Itisanticipatedthatallphasesofthisprojectwillbepermitted,installed,andoperationalwithin5yearsofbeginningconstruction.Athoroughanalysisofthecurrentscopeoftheentirefacilityandplannedoperationsindicatesthatallphasestogetherdonottriggermajornewsourcereview(majorNSR)permitting,alsocalledpreventionofsignificantdeterioration(PSD)permitting.AdescriptionofeachsourcecategoryapplicabletothecurrentprojectcanbefoundinSection2.AprocessflowdiagramfortheplannedPhase1operationsisincludedinAttachmentF.
1.2. R-13 APPLICATION ORGANIZATION
ThisR‐13permitapplicationisorganizedasfollows:> Section2:SampleEmissionSourceCalculations;> Section3:R‐13ApplicationForms;> AttachmentA:BusinessCertificate;> AttachmentB:AerialMap;> AttachmentC:InstallationandStartUpSchedule;> AttachmentD:RegulatoryApplicabilityDiscussion;> AttachmentE:PlotPlan;> AttachmentF:DetailedProcessFlowDiagram;> AttachmentG:ProcessDescription;> AttachmentH:MaterialSafetyDataSheets> AttachmentI:EmissionUnitsTable;> AttachmentJ:EmissionPointsDataSummarySheet;> AttachmentK:FugitiveEmissionsDataSummarySheet;> AttachmentL:EmissionsUnitDataSheets;> AttachmentM:AirPollutionControlDeviceSheet;> AttachmentN:SupportingEmissionCalculations;and> AttachmentO:Monitoring/Recordkeeping/Reporting/TestingPlans.
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2. SAMPLE EMISSION SOURCE CALCULATIONS
Aspartofthefirstphaseoftheproject,P&Gproposestoinstallequipmentinseveraldistinctmanufacturingareas:
SurfactantManufacturing; LiquidSoapMakingAandB; DryConsumerProductsA; SiteSupportingUtilities;and PlasticsMoldingSuppliers.
Eachofthesebusinessareaswillbediscussedingreaterdetailinthissection.AprocessflowdiagramisincludedasAttachmentF.Theinstallationofequipmentatthefacilitywillbeinstalledinmorethanonephase.Thebusinessareascontainedinthispermitapplicationmakeupphase1.Additionalphaseswillbepermittedatalaterdate.Itisanticipatedthatallphasesofthisprojectwillbepermitted,installed,andoperationalwithin5yearsofbeginningconstruction.Inaddition,thecharacteristicsofexpectedsiteairemissions,alongwiththemethodologyusedforcalculatingemissionsfromtheproposednewsources,aredescribedinnarrativeformbelow.TheTablerStationfacilityhasthepotentialtoemitthefollowingpollutants:
> Oxidesofnitrogen(NOX);> Sulfurdioxide(SO2);> SulfurTrioxide(SO3);> Carbonmonoxide(CO);> SulfuricAcid(H2SO4);> Volatileorganiccompounds(VOC);> Hazardousairpollutants(HAP);> Particulatematter(PM);> Particulatelessthan10micrometers(PM10);and> Particulatelessthan2.5micrometers(PM2.5).
DetailedsupportingcalculationsarealsoprovidedinAttachmentN.
2.1. SURFACTANT MANUFACTURING
2.1.1. Process Description
P&Gproposestoinstallequipmenttomanufacturesurfactants.Thepurposeofthesurfactantmakingoperationisprimarilytomanufacturesurfactantpastesusedintheliquidsoapmanufacturingprocesswhichisalsoincludedinthisapplication.Asecondarybyproductproducedbythesurfactantprocessisaprecipitatedacidmix(PAM).Similarly,anumberofvariationstothesurfactantpasteproductareintended,basedontheenduse.Thesevariationsareachievedthroughtheuseofvaryingrawmaterialsindifferentquantitiesinthesurfactantmanufacturingprocess.Withthestartupofthesurfactantprocess,itisnecessarytopreheatthesulfurreactors,whichisaccomplishedwiththeuseoffour(4)naturalgaspreheaters;Startupisintendedtooccurapproximatelyfour(4)timesperyearperreactor.Gassesfromthepreheaters(onlyusedduringstartup)areventedtothecommonstack.Duringstartup,anySO3producedwillbeventedtotheSO3absorberandthenthroughtheSO2scrubber.Rawsulfurisstoredinsulfurtanks.Gasesfromthecombustionofsulfur(normaloperation)areventedthroughaSO2packedbedscrubber.Duringchangeover,theSO3isventedtotheSO3absorber,andexhaustgasisventedthroughtheSO2scrubber.Abyproductproducedduringchangeoverperiodsissulfuricacid(H2SO4).
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Thesurfactantprocessesareanticipatedtoemitthefollowingcriteriapollutants:SO2,VOC,PM10,andPM2.5.
Additionally,asmallamountofNOX,CO,SO2areanticipatedtobeemittedthroughthepreheatingofthesulfurreactorusinganaturalgaspreheaterand/ortheoxidationofsulfurinvolvedinmakingthesurfactantpaste.Allsurfactantpotentialemissions,withtheexceptionofthenaturalgaspreheaters,areventedthroughaSO2packedbedscrubber.Additionally,VOCemissionsareanticipatedfromrawmaterialandproducttanks,inlinemixingtanks,andrailandtruckloading.EmissionsarecalculatedforthesurfactantmanufacturingcanbefoundinAttachmentN.Proposedemissionsourcesinthesurfactantprocessesincludethefollowing:
Rawmaterial,intermediate,andproducttanks; Naturalgaspreheatersandsulfurreactors; In‐linemixingand/ormixingtanks;and Producttruckloading.
TheproposedsurfactantprocesswillbecontrolledwiththefollowingequipmenttocontrolSO2andPMemissions:
PackedbedscrubberAdditionalinformationrelatedtocontroldevicescanbefoundinAttachmentM.
2.1.2. Emissions Calculations
2.1.2.1. Scrubber for Surfactant Manufacturing
TheTablerStationfacilitywillemitNOx,SO2,VOC,H2SO4,andPMthroughapackedbedSO2scrubberasaresultofsurfactantmanufacturing.ThepotentialtoemitforVOCisderivedfromthestacktestdatarecordedbysimilarP&Gsites.TheNOx,SO2,PM10,andPM2.5emissionratesarecalculatedusingemissionfactorssuppliedbythemanufacturer.Duringlimitedstartupperiods,naturalgaspreheatersareruntopreheattheprocessfromacoldstart;emissionsarecalculatedusingAP‐42emissionfactors.
AmajorityofthesulfurburnedistransformedintoSO3,absorbedandconvertedintofinishedproductinthesurfactantmakingprocess.However,afractionoftheSO2isnotconvertedtoSO3andnotalloftheSO3isconsumedinthereaction.TheexcessSO2isnotemitted;itiscontrolledbytheSO2scrubbers.Inthepresenceofwatervapor,SO3becomesdropletsofH2SO4(i.e.sulfuricacidmist).H2SO4dropletscontributetothecondensablefractionofPM10andPM2.5emissions.ForpurposesofthisapplicationitwasassumedthatthePM10andPM2.5emissionsfromthescrubberduringnormaloperationswereequaltotheresidualSO3fromthescrubber(which,inthepresenceofwatervaporisH2SO4).
2.1.2.2. Vertical Fixed Roof Tank Emission Calculation Methodology
TheproposedTablerStationprojectincludestanksineachoftheproposedprocessareas.MonthlyVOCemissionsfromfixedrooftanksarecalculatedusingproceduresinAP‐42Section7.1.
Fixedrooftankstypicallyhavetwomajortypesofemissions:workinglossesandbreathinglosses.Workinglossesoccurduringtheday‐to‐dayoperationsofthetankfromthereleaseofthevaporspaceasthetankisfilledandemptied.Breathinglossesoccuratoutdoorambienttanksthataresubjecttodailytemperaturechangeswiththeweather.AmajorityofthetanksattheTablerStationfacilityaretemperaturecontrolledand,assuch,donothavebreathinglosses.Breathinglosseswerecalculatedforambientoutdoortanks.
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ThetanksattheTablerStationfacilitycontainavarietyoforganicmaterialsusedinthemanufactureofsurfactants,liquidsoap,anddryconsumerlaundryandcleaningproducts.Emissionsfromtankscontainingrawmaterialswerecalculatedusingthespecificpropertiesofthatmaterial.EmissionsfromtankscontainingintermediatematerialsormixtureswerecalculatedusingRaoult’slaw1andthepropertiesofthemostvolatilecomponentofthemixture.MinorcomponentsofrawmaterialHAPhavebeenincludedinindividualmaterialusagetankcalculations,asapplicable.HAPamountsinrawmaterialsbasedonreviewofMaterialSafetyDataSheets.
2.1.2.3. Liquid Material Handling
AsdiscussedinSection2.1.2.2,severaloftheproductsandprocessesattheTablerStationfacilitycontainorganicliquidswitharangeofvolatility.FugitiveemissionsofVOCthatoccurduringthemixingofrawmaterials,intermediatesandproducts;ortransferandpackagingofproducts,arecalculatedthroughtheuseofaworkinglossequation;thisequationcalculatestheemissionsthatresultfromlostvaporsduetoliquidmovementwhentanksarebeingfilledoremptiedandcanbefoundinAP‐42Section7.1asEquation1‐29.Thisworkinglossduetoliquidmovementissimilartowhatoccurswhenmixingorpackagingliquidrawmaterials,intermediates,andproductsandthereforeisusedforestimatingtheassociatedemissionrate.
2.1.2.4. Truck Loading and Unloading
ThetransferoforganicchemicalsintoandoutoftruckswilloccurasapartoftheoperationsattheTablerStationfacility.IntermediatesandfinalproductsthatareloadedintotrucksproducevaporscontainingVOC,HAPandH2SO4.Theemissionsfromunloadingoftrucksisaccountedforintheworkinglossesofthetanks.TheemissionsfromtheloadingoftrucksarecalculatedusingEquation1inAP‐42Section5.2.Asaturationfactorof0.6isselectedbasedonTable5.2‐1ofAP‐42Section5.1forbottom/submergedloadingofatruckduringnormalloadout.VOCconcentrationisassumedtobe100%whereasHAPandH2SO4varybystream.
2.2. LIQUID SOAP MAKING A AND B
2.2.1. Process Description
P&GalsoproposestoinstallLiquidSoapAandBmanufacturingprocesses.BothSoapAandSoapBmanufacturingprocessesinvolveprimarilymixingoperationswithnochemicaltransformations.Therawmaterialsprimarilyconsistofbutarenotlimitedtodyes,perfumes,surfactantsessentialforsoapmanufacturing,andminorcomponentadditivesintendedtodeliverproductperformanceattributes.Liquidrawmaterialswilleitherbepipedfromelsewhereon‐siteorbetransportedtothesiteintotes/drumswhichwillbeunloadedintothebuildingforplacementintothemixingtanks.Dryrawmaterialswillbeweighedonascalebeforebeingmanuallyaddedtothemixingtanks.LiquidSoapAisavariationoftheproductthatmaycontainahighervolatilityprocessingaid,dependingonproductformulation.Thehighervolatilityprocessingaidmaybeprocessedhotoratambienttemperature.WhenLiquidSoapAisbeingmanufacturedhotandthehighervolatilityprocessingaidisused,volatileemissionsfromthemixingtankswillberoutedthrougharegenerativethermaloxidizer(RTO).WhenLiquidSoapAisbeingmanufacturedatambienttemperatureandthehighervolatilityprocessingaidisused,volatileemissionsfromthemixingtanksarenotcontrolled.LiquidSoapBdoesnotcontainthehighervolatilityprocessingaidandwillnothaveemissionsroutedthroughtheRTO.
1 The partial vapor pressure of each component of an ideal mixture of liquids is equal to the vapor pressure of the pure component multiplied by its mole fraction in the mixture.
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Theresultantmixturerepresentsthefinalproduct.Variationsofthemixturearedependentuponthesoapproducttobemanufactured.Theproduct,oncemade,ispipedintoapackinglineforfillingcontainers.Afterfilling,theproductwillproceedtofinalpackagingforoff‐sitetransport.Aspartofqualityassurance,processtanksandliquidfillingequipmentisperiodicallycleanedandsanitizedusinghotwater.Residualrawmaterialrelatedemissionsthatmayoccurduringcleaningandsanitizationareaccountedforinstorageandprocesstankemissionscalculations.Theemissionsourcesfortheliquidsoapmanufacturingprocessincludes:
Storingrawmaterialsintanks,totes,ordrums Weighingandmixingrawmaterials Productpackaging
EmissioncalculationsforLiquidSoapAandBmanufacturingcanbefoundinAttachmentN.TheproposedliquidsoapprocesseswillbecontrolledwiththefollowingequipmenttocontrolVOCandPMemissions:
RegenerativeThermalOxidizer(RTO)(LiquidSoapAonly);and Rotoclones,liquid(water)scrubbers.
AdditionalinformationrelatedtothesecontroldevicescanbefoundinAttachmentM.Asdiscussedinthenextsection,perfumemaybeusedintheLiquidSoapA&Bmakingprocess.Asmallquantityofperfumemaybeemitted,amongothervolatileorganiccompounds,asafugitive.AdditionalinformationcanbefoundinAttachmentN.7
2.2.2. Emissions Calculations
EmissionscalculationmethodologyfortanksandpackaginghasalreadybeendiscussedinSections2.1.2.2and2.1.2.3,respectively.Thissectionwilldiscusstheemissionscalculationsfortheprocesstanks.
2.2.2.1. Process Tanks
TheprocesstanksforLiquidSoapAandBmanufacturingareequippedwithrotoclonesfordustcontrol.Inaddition,someoftheprocesstanksforLiquidSoapAareequippedwithanRTO.PM,PM10,andPM2.5emissionsfromtherotoclonesarecalculatedbasedongrainloadingbasedonP&Gprocessknowledge.ItisconservativelyassumedthatPM10andPM2.5emissionsareequaltoPMemissions.TheVOCemissionsfromtheprocesstanksforLiquidSoapAandBarecalculatedbasedonP&Gprocessknowledge.TheRTOemissionfactorsarebasedonamassbalanceofVOC,vendorguarantees(NOX,CO),andAP‐42factors(PM10,PM2.5,SO2).
2.3. DRY CONSUMER LAUNDRY AND CLEANING PRODUCTS A
2.3.1. Process Description
Additionally,P&GproposestoinstallmanufacturinglinestomanufactureDryConsumerLaundryandCleaningProducts.Theprocessincludesdeliveryofrawmaterialsandtransferofmaterialtodayandmixingtanks.Themixtureisthenappliedontoasubstratetoproducethefinalproduct.Thefinalproductistrimmedtosize,packaged,andsenttoawarehousefordistribution.Variousprocessinglinesareinvolvedwithmanufacturingcleaningarticlesintothedifferentconsumercleaningproducts.Thesourcesofemissionsincludethefollowingequipment:
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Rawmaterialtanks Intermediatemixing Additionofliquidrawmaterials Finishedproductpackaging
EmissionsestimatesarebasedontherawmaterialswiththehighestvaporpressuretoaccountforthepotentialVOCemissionstorepresentthemultipleformulationsinthecleaningarticlemanufacturingprocess.EmissionsestimatescanbefoundinAttachmentN.TheproposedDryConsumerLaundryandCleaningProductsprocesswillbecontrolledwiththefollowingequipmenttocontrolparticulateemissions:
BaghousesandbinventfiltersAdditionalinformationrelatedtothesecontroldevicescanbefoundinAttachmentM.Asdiscussedinthenextsection,asmallamountofperfumemaybeincludedintheproductformulation.Emissionpointswiththepotentialtoemitodor,suchastheareawereliquidrawmaterialsareadded,arecontrolledwithactivatedcarbon.Theactivatedcarbonservesasacontrolforemployeecomfortandtopreventnuisanceodors,ratherthanforcriteriapollutants,suchasVOC.Assuch,itwillnotbeconsideredacontroldeviceinthisapplication.
2.3.2. Emissions Calculations
EmissionscalculationmethodologyfortanksandintermediatemixingtankshasalreadybeendiscussedinSections2.1.2.2and2.1.2.3,respectively.Thissectionwilldiscusstheemissionscalculationsfortheadditionofliquidrawmaterialsandparticulateemissionscontrolforfinishedproductpackaging.
2.3.2.1. Addition of Liquid Raw Materials
TheDryConsumerLaundryandCleaningProductsAprocessproducesavarietyofconsumergoods,allofwhichbeginwithasubstrate.Thissubstratemayreceiveavarietyofliquidrawmaterialsintendedtoenhancetheperformanceandfunctionalityoftheconsumerproduct.Therawmaterialstypicallyconsistoflow‐volatile,highmolecularweightorganicmaterialspairedwithasmallamountofperfume.Aftertherawmaterialsareapplied,thesubstrateiscuttosize,andpackaged.AsmallamountofVOCemissionswillresultfromtheapplicationprocessandsubsequentexposedsubstratesurface.Regardlessofthetypeofmaterialappliedorsubstrateused,emissionsevaporatingfromthesubstratewilldispersesimilartoemissionsevaporatingfromaresidual“puddle”,whichprovidesaconservativeestimateofpotentialemissions.Theareaoverwhichemissionscouldpotentiallydischargeintotheatmosphereisthesameastheareaoverwhichrawmaterialswouldbeappliedandthereforevariesbasedontheapplicationprocess.TheevaporationandemissionsofVOCcanbeestimatedusingthefollowingequationfoundinEPA’s2007EmissionInventoryImprovementProgram’sTechnicalReportSeriesVolumeIISection16,pages49‐50.
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EM K AP
RT
Where:
En = Evaporationrateofthevolatilecomponent
Mn = Molecularweightofthevolatilecomponent
Kn = Masstransfercoefficient
A = Surfaceareaofsubstrateexposed ft Pnsat = Saturatedsolventvaporpressure psia
R = Universalgasconstant 10.73
°
TL = Absolutetemperatureoftheliquid (˚R)
ThemasstransfercoefficientfortheVOCmixtureisrelatedtoareferencecompound,inthiscasewater,throughthefollowingequation.
KK
MM
Where:
Kn = MasstransfercoefficientofVOCmixture
K0 = Masstransfercoefficientofwater 98.03
Mn = Molecularweightofthevolatilecompound
M0 = Molecularweightofwater 18
TheareaoverwhichVOChavethepotentialtoevaporateisrelatedtotheapplicationprocessofthevolatilematerial.Therefore,thespillareaisequaltothesurfaceareaofthelinefromthepointofapplicationofthevolatilematerialuntilthesubstrateiswoundforstorage.
A L ∗ W Where: A = Areaoftherepresentative“puddle” ft Ll = Lengthoftheline (ft) Wl = Widthoftheline (ft)
2.3.2.2. Particulate Emission Control for Raw Material Addition
BaghousesandfabricfiltersareproposedtocontrolparticulateemissionsforTablerStationintheDryConsumerLaundryandCleaningProducts.PM,PM10,andPM2.5emissionsfromthebaghousesarecalculatedbasedonfabricfiltergrainloadingandbaghouseflowratesbasedonP&Gprocessknowledge.ItisconservativelyassumedthatPM10andPM2.5emissionsareequaltoPMemissions.
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2.4. UTILITIES
2.4.1. Process Description
Tosupporttheheating,cooling,ventilation,andsteamneedsfortheprocessesthatarebeingproposedwiththisproject,P&Gisproposingtoinstallthefollowingequipment:2
Two(2)50,267poundperhour(pph)steamboilers One(1)25,134poundperhour(pph)steamboiler One(1)8,918poundperhour(pph)steamtemporaryboiler Six(6)naturalgasfiredbuildingheaters Three(3)coolingtowers
Theboilerswillbefueledprimarilybynaturalgas.Thepurposeoftheboilersistosupplyheatorsteam.Thetemporaryboilerwillbeamobileunitthatwillprovidesupporttoplantprocessesasthemainfacilityboilersareinstalled.Thetemporaryboilerwillnotberunatthesametimeasthemainfacilityboilers.Emissionsfromthetemporaryboilerwillbelessthanemissionsfromthemainfacilityboilers.Thepurposeofthebuildingheatersistoprovidecomfortheatingforthewarehouseandotherbuildings.Thecoolingtowersareforbothcomfortandprocesscoolingwatersupplytobuildingsandmanufacturingequipmentassociatedwiththevariousprocesses.Tobepreparedforpoweroutagesandtobeequippedtoquicklyrespondtofires,thefollowingequipmentisalsoproposedbeinstalled:
Three(3)350KWstandby/backupelectricgeneratorswithdieselengines Two(2)311horsepower(HP)firepumpswithdieselengines
Thestandby/backupgeneratorandfirepumpengineswillbefueledwithULSDandmeetU.S.EPA’sTier3specifications.Additionally,theplantintendstoinstallfivedieseltanks,lessthan500gallons,tosupplythestandby/backupgeneratorsandfirepumpengines.Also,adieselrefuelingstationtosupplyon‐sitemobileequipmentisproposedtobeinstalled.Thefollowingfueltankswillbeinstalledatthesite:
5,000gallonULSDtankforvehiclerefuelingTheTablerStationfacilityintendstoinstallawaterpretreatmentsystemaswellasawastewaterpretreatmentsystem.Thewaterpretreatmentsystemwillpurifyandsoftenthewaterbeforeusetomaintainproductquality.Thewastewatersystemwillusechlorinationandotherprocesstocleanthewastewaterbeforedischargetothesanitarysewer.EmissionscalculationsfortheabovelistedequipmentareenclosedinAttachmentNoftheapplication.Emissionshavebeenestimatedusingeithervendorsuppliedspecifications,applicableAP‐42factors,and/ormassbalanceequationsassociatedtothetypeofemissionssourcelistedabove.
2 Final sizes and numbers of equipment in the utilities area subject to change.
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2.4.2. Emissions Calculations
2.4.2.1. Boilers
CO,VOC,PM10,PM2.5,SO2andleademissionsfromtheproposedboilersarecalculatedusingtheemissionfactorsfoundinAP‐42Section1.4(naturalgas),exceptwhereamanufacturer’sguaranteeapplies.TheH2SO4emissionfactorwascalculatedbyassumingonepercentofthesulfurcontainedwithinthenaturalgasisemittedassulfuricacid.3
2.4.2.2. Standby/Backup Generators and Fire Pump
ThethreegeneratorenginesandtwofirepumpenginesproposedfortheTablerStationfacilitywillbesubjecttotheemissionlimitationsinNSPSSubpartIIII(thegeneratorwillonlybesubjecttothenotificationrequirementsofNESHAPZZZZ).Toverifycompliancewiththesestandards,emissionsfromtheenginesarecalculatedbasedonemissionsfactorsprovidedbythemanufacturers.Sincethisequipmentwillonlyoperateduringemergencysituationsandroutinemaintenanceandtesting,annualemissionsarecalculatedbasedon500hoursofoperations.
2.4.2.3. Heater Emissions
Theproposedprocessheaterswillbefiredonnaturalgas.EmissionfactorsforNOx,CO,PM,PM2.5,PM10,SO2,lead,andVOCfromAP‐42Section1.4wereused.TheH2SO4emissionfactorwascalculatedbyassumingonepercentofthesulfurcontainedwithinthenaturalgasisemittedassulfuricacidinthesamemannerasfortheboilers.
2.4.2.4. Cooling Towers
TheTablerStationfacilityincludesthreecoolingtowers.TheanticipatedpollutantsarePM,PM10,andPM2.5.PotentialhourlyemissionsfromthecoolingtowerarecalculatedusingthemethodologyinAP‐42Section13.4‐1.
2.4.2.5. Water and Wastewater Pretreatment
TheTablerStationfacilitywillhavewaterpretreatmentonsitetomaintainthequalityofthecoolingtowerandboilerfeedwater.Inaddition,thefacilitywillhavepretreatmentprocessesforthewastewater.Theequipmentintheseareasmayincludetanksforwastewatercollectionandtreatmentandtotesoftreatmentchemicals.Processesmayincludeadissolvedairflotationunit,physicalandchemicalpretreatment,biologicaltreatment,andsettlingtanks.Emissionswerecalculatedusinganengineeringestimateoftheamountofeachtreatmentchemicalusedanditsvolatileand/orhazardouscontent.
2.5. PLASTICS MOLDING
2.5.1. Process Description
TheTablersStationfacilitywillincorporatethirdpartysupplierswhowillprovideaplasticsmoldingprocessforthemanufactureofbottles,caps,andotherformedplasticparts.
3 Emergency Planning and Community Right-To-Know Act, EPCRA - Section 313: Guidance for Reporting Sulfuric Acid (acid aerosols including mists, vapors, gas, fog, and other airborne forms of any particle size). (March 1998) EPA-745-R-97-007.
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Theplasticbottleandcapmakingprocessinvolvesinjectionmolding,blowmolding,andextrusionblowmolding.Theprocessstartswiththeunloadingofplasticpelletsfromrailcarsintostoragesilos.Fromthesilos,thepelletsarepipedtopressesandmoldingmachineswhichmakebottles,capsandotherformedplasticpartsdependingonproductneeds.Thepressesandmoldingmachinesheattheplasticwithelectricalheatersandviafrictionheating.Scrapplasticisregroundandreuseddirectlyinthemakingprocess.EmissionscalculationsfortheabovelistedequipmentareenclosedinAttachmentNoftheapplication.EmissionshavebeenestimatedusingeithervendorsuppliedspecificationsorapplicableAP‐42factors.
2.5.2. Emissions Calculations
2.5.2.1. Dry Material Handling
Plasticpelletsarestored,conveyedandground.Particulateemissionsfortheseareasareestimatedbythesupplierbasedontheaverageofpublishedfactorsavailableforothertypesofpelletstorage,includinggrainandwoodpellets.
2.5.2.2. Fugitive VOC
WhentheplasticpelletsareheatedtobepressedormoldedtheyemitasmallquantityofVOC.TheVOCemittediscalculatedusingafactorfromafactsheetfromtheMichiganDepartmentofEnvironmentalQualityentitled“PlasticsProductionandProductsManufacturing”(#9847,revisedNovember2005).TheotherfugitiveVOCsarefromcleaningproductsandarecalculatedassuming100%lossrateofvolatilecomponentsofcleaningproducts.
2.6. PLASTICS MOLDING UTILITIES
2.6.1. Process Description
Tosupporttheheating,cooling,andventilationneedsfortheplasticsmoldingsuppliers,P&Gisproposingtoinstallthefollowingequipment:4
Six(6)naturalgasfiredbuildingheaters; One(1)coolingtower;and One(1)70kWstandby/backupelectricgeneratorwithnaturalgasengine.
Thepurposeofthebuildingheatersistoprovidecomfortheatingforthewarehouseandotherbuildings.Thecoolingtowerisforbothcomfortandprocesscoolingwatersupplytobuildingsandmanufacturingequipmentassociatedwiththevariousprocesses.Thebackupelectricgeneratoristobepreparedforpoweroutages.EmissionscalculationsfortheabovelistedequipmentareenclosedinAttachmentNoftheapplication.Emissionshavebeenestimatedusingeithervendorsuppliedspecifications,applicableAP‐42factors,and/ormassbalanceequationsassociatedtothetypeofemissionssourcelistedabove.
4 Final sizes and numbers of equipment in the utilities area subject to change.
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2.6.2. Emissions Calculations
Emissionscalculationmethodologyfornaturalgasheaters,andcoolingtowershasalreadybeendiscussedinSection2.4.2.Thissectionwilldiscusstheemissionscalculationsforthenaturalgasenginethatpowersthestandby/backupelectricgenerator.
2.6.2.1. Standby/Backup Generator and Fire Pump
ThegeneratorengineproposedfortheTablerStationfacilitywillbesubjecttotheemissionlimitationsinNSPSSubpartJJJJ.Toverifycompliancewiththesestandards,emissionsfromtheenginesarecalculatedbasedonemissionsfactorsprovidedbythemanufacturers.Sincethisequipmentwillonlyoperateduringemergencysituationsandroutinemaintenanceandtesting,annualemissionsarecalculatedbasedon500hoursofoperations.
2.7. SOURCES OF MINOR SIGNIFICANCE
Eachoftheprocessareas(surfactants,liquidsoapAandB,dryconsumerlaundryandcleaningproductsA,utilities,andplasticsmolding)containemissionsunitsthatProcterandGambledefinesas“sourcesofminorsignificance”.SomeofthesesourcesarealreadydefinedasdeminimissourcesbyDEPin45CSR13,Table45‐13b,suchashaulroademissions,labvents,andwelding.Additionalsources,withemissionslessthan0.5tpyofanypollutant,suchastanksstoringmaterialswithalowvolatility,havebeenaddedtoalistof“sourcesofminorsignificance”.Alistofthesesourcescanbefoundinpage2ofAttachmentI.
P&G – Tabler Station | R13 Permit Trinity Consultants 14
3. R13 APPLICATION FORM
TheDEPpermitapplicationformscontainedinthisapplicationincludeallapplicableR‐13applicationformsincludingtherequiredattachments.
P&G – Tabler Station | R13 Permit Trinity Consultants
ATTACHMENT A
Current Business Certificate
P&G – Tabler Station | R13 Permit Trinity Consultants
ATTACHMENT B
Aerial Map
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Attachment B - Aerial Map
UTM Easting (m)
UTM
North
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All coordinates shown in UTM projection,Zone 17, NAD 83
Area Map Extent
Tablers Station Location
Procter and Gamble
P&G – Tabler Station | R13 Permit Trinity Consultants
ATTACHMENT C
Startup and Installation Schedule
Attachment CTabler Station
Unit InstallationSchedule StartupScheduleSurfactantMakingLiquidSoapAandB
DryConsumerProductsAUtilities
December2016 April2017
PlasticsMoldingAreaPlasticsMoldingUtilities
December2016 August2017
AttachmentCScheduleofPlannedInstallationandStart‐Up
Page 1 of 1Trinity Consultants
141801.0078
P&G – Tabler Station | R13 Permit Trinity Consultants
ATTACHMENT D
Regulatory Applicability Discussion
P&G|AttachmentDTrinityConsultants 1
ATTACHMENT D – REGULATORY APPLICABILITY
ThissectiondocumentstheapplicabilitydeterminationsmadeforFederalandStateairqualityregulations.Themonitoring,recordkeeping,reporting,andtestingplanispresentedinAttachmentO.Inthissection,applicabilityornon‐applicabilityofthefollowingregulatoryprogramsisaddressed:
> PreventionofSignificantDeterioration(PSD)permitting;> MinorNewSourceReview;> TitleVofthe1990CleanAirActAmendments;> NewSourcePerformanceStandards(NSPS);> NationalEmissionStandardsforHazardousAirPollutants(NESHAP);and> WestVirginiaStateImplementationPlan(SIP)regulations.
Thisreviewispresentedtosupplementand/oraddclarificationtotheinformationprovidedintheWestVirginiaDepartmentofEnvironmentalProtection(DEP)Rule13(R‐13)permitapplicationforms.Inadditiontoprovidingasummaryofapplicablerequirements,thissectionoftheapplicationalsoprovidesnon‐applicabilitydeterminationsforcertainregulations,allowingtheDEPtoconfirmthatidentifiedregulationsarenotapplicabletotheproposedproject.Notethatexplanationsofnon‐applicabilityarelimitedtothoseregulationsforwhichtheremaybesomequestionofapplicabilityspecifictotheoperationsattheTablerStationfacility.Regulationsthatarecategoricallynon‐applicablearenotdiscussed(e.g.,NSPSSubpartJ,StandardsofPerformanceforPetroleumRefineries).
Prevention of Significant Deterioration (PSD) Source Classification
FederalconstructionpermittingprogramsregulatenewandmodifiedsourcesofattainmentpollutantsunderPSDandnewandmodifiedsourcesofnon‐attainmentpollutantsunderNon‐AttainmentNewSourceReview(NNSR).TheTablerStationfacilitywillbelocatedinBerkeleyCounty,WestVirginia,whichisdesignatedasinattainment/unclassifiableforallpollutants.Therefore,PSDpermittingispotentiallyapplicabletothefacility.PSDpermittinginWestVirginiaisregulatedunderTitle45,Series14,WestVirginiaCodeofStateRegulations(45CSR14).PSDpermittingappliestoconstructionofnewmajorstationarysourcesoranyphysicalchangein,orchangeinthemethodofoperationofanexistingmajorstationarysourcethatresultsinasignificantemissionsincrease.AmajorstationarysourceforPSDisdefinedas:> Anysourceinoneofthelistedsourcecategoriesinthedefinitionof“majorstationarysource”per45CSR14‐2.43
withthepotential‐to‐emit(PTE)of100tonsperyear(tpy)ormoreoftraditionallyregulatedpollutants,or> AnysourcenotinoneofthelistedsourcecategorieswithaPTEof250tpyormoreofanytraditionallyregulated
pollutant.AreviewofthelegislativebackgroundandPSDregulationsdoesnotclearlyindicateSICasthedefiningfactorforcategorizationofafacilityasachemicalprocessplant.However,EPAhashistoricallyinterpretedthecategory“chemicalprocessplants”asincludinganyactivitylistedunderSICmajorgrouping28(witharecentspecificexceptionforethanolproductionfacilities).SIC28hasabroaderscopethansiteswherechemicalprocessesareoccurring,asSIC28isdefinedasChemicalsandAlliedProducts,andnotsimplychemicals.TheAlliedProductsportionofSIC28includesmultipleactivitieswherethereisnochemicalprocessingatall,suchasphysicalblendingofingredientstomakefinishedchemicalproductstobeusedforultimateconsumptionsuchasdrugs,cosmetics,andsoaps[citedfromSIC28definition].MostoftheproposedsitewouldbeclassifiedunderSIC284,SOAP,DETERGENTS,ANDCLEANINGPREPARATIONS,PERFUMES,COSMETICS,ANDOTHERTOILETPREPARATIONS
P&G|AttachmentDTrinityConsultants 2
FollowingEPA’shistoricdetermination,thesenon‐chemicalprocessareaswouldbeconsideredtobechemicalprocessplants,andthusthefacilityfallsintothegroupofsourcecategoriessubjecttoa100tpymajorsourcethreshold.Becausethefacility‐widePTEforeachpollutantislessthan100tpy,theTablerStationfacilitywillbeanewminorsourceunderPSD.Assuch,PSDpermittingisnottriggeredbythisconstructionactivity. TheTablerStationfacilityisanticipatedtoincludeadditionalprocessareasaspartoftheoverallscopeoftheTablerStationproject.Anyadditionalprocessareasrelatedtotheprojectwhicharecurrentlyundergoingdetaileddesignwillbepermittedatalaterdate.Itisanticipatedthatallphasesofthisprojectwillbepermitted,installed,andoperationalwithin5yearsofbeginningconstruction.AthoroughanalysisofthecurrentscopeoftheentirefacilityandplannedoperationsindicatesthatallphasestogetherdonottriggerPSDpermitting.
Minor New Source Review Source Classification
Theminor(orstate)NSRprogramiscodifiedin45CSR13,andistypicallyknownasanR‐13permit.TheproposedTablerStationfacilitydoesnotqualifyforanycategoricalexemptions,andthusthepotentialemissionrateforthefacilityiscomparedagainsttheemissionthresholdin45CSR13‐2.24(b)and45CSR13‐2.24(b).AscalculatedinAttachmentN,theproposedprojecttriggersminorNSRforPM,PM10,PM2.5,VOC,NOX,CO,andHAP.IncompliancewithR‐13,P&GissubmittingtheattachedpermitapplicationfortheinstallationofaconsumerproductsfacilityatTablerStation,WestVirginia.
Title V Operating Permit Program
Title40oftheCodeofFederalRegulationsPart70(40CFR70)establishesthefederalTitleVoperatingpermitprogram.WestVirginiahasincorporatedtheprovisionsofthisfederalprograminitsTitleVoperatingpermitprogramin45CSR30.ThemajorsourcethresholdswithrespecttotheWestVirginiaTitleVoperatingpermitprogramregulationsare10tonsperyear(tpy)ofasingleHAP,25tpyofanycombinationofHAPs,and100tpyofallotherregulatedpollutants.1ThepotentialemissionsofVOCarebelowthe100tpythresholdatthisfacility.Therefore,theTablerStationfacilityisnotamajorsourceforTitleVpurposes.
New Source Performance Standards
NSPSrequirenew,reconfigured,orreconstructedsourcestocontrolemissionstothelevelachievablebythebestdemonstratedtechnologyasspecifiedintheapplicableprovisions.Moreover,anysourcesubjecttoanNSPSisalsosubjecttothegeneralprovisionsofNSPSSubpartA,unlessspecificallyexcluded.FollowingisadiscussionofpotentiallyapplicablesubpartsfortheproposedemissionsourcesattheTablerStationfacility.
NSPS Subpart A – General Provisions
AnysourcesubjecttoaNSPSisalsosubjecttothegeneralprovisionsofNSPSSubpartA,unlessspecificallyexcluded.
NSPS Subpart H – Sulfuric Acid Plants
NSPSSubpartHappliestosulfuricacidproductionunits,whicharedefinedas(emphasisadded):
1EPA’sTailoringRulehadestablishedaTitleVmajorsourcethresholdof100,000tpyofgreenhousegaspollutantsorGHGs(onacarbondioxideequivalent[CO2e]basis).However,onJune23,2014,theU.S.SupremeCourtissueditsdecisioninUtilityAirRegulatoryGroupv.EPA,wherebytheCourtsaidthatEPAmaynottreatGHGsasanairpollutantforpurposesofdeterminingwhetherasourceisamajorsourcerequiredtoobtainaPSDorTitleVpermit.CaseNo.12‐1146,decidedJune23,2014.http://www.supremecourt.gov/opinions/13pdf/12‐1146_4g18.pdf.
P&G|AttachmentDTrinityConsultants 3
(a) Sulfuricacidproductionunitmeansanyfacilityproducingsulfuricacidbythecontactprocessbyburningelementalsulfur,alkylationacid,hydrogensulfide,organicsulfidesandmercaptans,oracidsludge,butdoesnotincludefacilitieswhereconversiontosulfuricacidisutilizedprimarilyasameansofpreventingemissionstotheatmosphereofsulfurdioxideorothersulfurcompounds.2
ProcterandGambleintendstousethereactorsprimarilytoproducesurfactantforuseintheirproducts.ThesurfactantmakingprocessatTablerStationproducessulfuricacidtopreventsulfurdioxideemissionstotheatmosphere.Sulfuricacidistypicallyproducedduringtransitionperiodssuchasstartup,shutdown,orwhenareactorischangingovertoproduceadifferenttypeofsurfactant.However,becauseofthephasedstartupofthefacilityasawhole,ProcterandGambleanticipatesthattheremaybeperiodswhen,inordertofullyutilizetheequipment,areactormaybededicatedtosulfuricacidproduction.ThoughProcterandGamblehopestofindaninterestedbuyerforthesulfuricacid,thesulfuricacidwillnotbeproducedastheprimaryproductofthesurfactantmakingsystem.Sulfuricacidsalesarenotthefinancialobjectiveofthereactorinstallation.ThoughtheTablerStationfacilitywillproducesulfuricacid,itisnottheprimarypurposeofthesurfactantmakingoperation.Thesulfuricacidmakingisusedprimarilyasameansofpreventingsulfurdioxideemissionsfromenteringtheatmosphere,andwillnotgenerallybeproducedasastand‐aloneproduct.Therefore,theTablerStationfacilityisexemptfromSubpartH.
NSPS Subpart Dc – Steam Generating Units
TheNSPSSubpartDcapplicabilitydefinitionprovides:
(a) …theaffectedfacilitytowhichthissubpartappliesiseachsteamgeneratingunitforwhichconstruction,modification,orreconstructioniscommencedafterJune9,1989andthathasamaximumdesignheatinputcapacityof29megawatts(MW)(100millionBtuperhour(Btu/hr))orless,butgreaterthanorequalto2.6MW(10millionBtu/hr)3
Thethreemainboilersatthesitehavearatedheatinputcapacityof62MMBtu/hr,62MMBtu/hr,and31MMBtu/hrandaresubjecttothisrule.Inaddition,the11MMBtu/hrtemporaryboilerisalsosubjecttothisrule.Theboilerswillonlycombustnaturalgas.Therequirementsthatapplyfornaturalgasboilersaretorecordandmaintainrecordsoftheamountoffuelcombustedduringeachcalendarmonthandmaintaincertificationsfromthenaturalgassupplierguaranteeingsulfurcontentofthefuel.
NSPS Subpart Kb – Storage Tanks
NSPSSubpartKb,StandardsofPerformanceforVolatileOrganicLiquidStorageVessels,regulatesstoragevesselswithadesigncapacitygreaterthanorequalto75cubicmeters(m3)thatstorevolatileorganicliquids. Thestandardsareeffectiveforallfacilitiesforwhichconstruction,reconstruction,ormodificationcommencedafterJuly23,1984.Storagevesselswithacapacitygreaterthanorequalto151cubicmeters(m3) storingaliquidwithamaximumtruevaporpressure,excludingwater,lessthan3.5kilopascals(kPa)orwithacapacitygreaterthanorequalto75m3 butlessthan151m3 storingaliquidwithamaximumtruevaporpressurelessthan15.0kPaareexemptfromtherequirementsofthisrule. ThetanksattheTablerStationfacilitymeettheexemptionrequirementsofthisrule.Therefore,theTablerStationfacilityisexemptfromNSPSKb.
240CFR60.81340CFR§60.40c(a)
P&G|AttachmentDTrinityConsultants 4
NSPS VVa – SOCMI Equipment Leaks
Per40CFR60.480a(b),NSPSVVaappliestoanyaffectedfacilitythatcommencesconstruction,reconstruction,ormodificationafterNovember7,2006,whereanaffectedfacilityisthegroupofallequipmentwithinaprocess.Thedefinitionof“processunit”and“equipment”areasfollowsper40CFR60.480a(f)(2):
Processunitmeanscomponentsassembledtoproduce,asintermediateorfinalproducts,oneormoreofthechemicalslistedin§60.489ofthispart.Aprocessunitcanoperateindependentlyifsuppliedwithsufficientfeedorrawmaterialsandsufficientstoragefacilitiesfortheproduct.Equipmentmeanseachpump,compressor,pressurereliefdevice,samplingconnectionsystem,open‐endedvalveorline,valve,andflangeorotherconnectorinVOCserviceandanydevicesorsystemsrequiredbythissubpart.
Theonlychemicalproducedeitherasafinalproductorasanintermediatefromthelistgivenin§60.489ofthispartattheTablerStationfacilityisdioxane(CAS#123‐91‐1),anunintendedbyproductproducedduringthesurfactantmakingprocessataverylowconcentration.Therefore,P&Ghasapotential“processunit”asdefinedunderNSPSVVa.ForpurposesofcompliancewithNSPSVVa,the“affectedfacility”isthegroupofallequipmentwithinthesurfactantsprocessunit.ThisprocessunitwillbeconstructedafterNovember7,2006.Assuch,thegroupofallequipmentinthesurfactantsprocessunitissubjecttotherequirementscodifiedinNSPSVVa.Per40CFR60.480a(d),thefollowingexemptionsareavailableunderNSPSVVa:
> Anyaffectedfacilitythathasthedesigncapacitytoproducelessthan1,000Mg/yr(1,102ton/yr)ofachemicallistedin§60.489isexemptfrom§§60.482–1athrough60.482–11a.
> Ifanaffectedfacilityproducesheavyliquidchemicalsonlyfromheavyliquidfeedorrawmaterials,thenitisexemptfrom§§60.482–1athrough60.482–11a.
> Anyaffectedfacilitythatproducesbeveragealcoholisexemptfrom§§60.482–1athrough60.482–11a.> AnyaffectedfacilitythathasnoequipmentinVOCserviceisexemptfrom§§60.482–1athrough60.482–11a.
TheP&Gsurfactantmakingprocessproducesdioxaneinextremelysmallquantitiesasanunintendedbyproduct.Lessthan1,000Mg/yearofdioxaneisproduced;thereforetheTablerStationfacilityqualifiesforthefirstexemption.Assuch,P&Gdoesnotoperatean“affectedfacility”underNSPSVVaand,assuch,P&Gisnotsubjecttotherequirementslistedin§§60.482−1athrough60.482–11a.However,P&Gisrequiredtokeeprecordsonsitetodocumenttheexemption.
NSPS III – SOCMI Air Oxidation Reactor
Per40CFR60.610(a),NSPSIIIappliestoeachaffectedfacilitythatispartofaprocessunitthatproducesanyofthechemicalslistedin40CFR60.617asaproduct,co‐product,by‐product,orintermediate.Anaffectedfacilityisanyofthefollowingforwhichconstruction,modification,orreconstructioncommencedafterOctober21,1983:4
> Eachairoxidationreactornotdischargingitsventstreamintoarecoverystream;> Eachcombinationofanairoxidationreactorandtherecoverysystemintowhichitsventstreamis
discharged;or> Eachcombinationoftwoormoreairoxidationreactorsandthecommonrecoverysystemintowhichtheir
ventstreamsaredischarged.
“Airoxidationreactor”and“processunit”aredefinedin40CFR60.611asfollows:
440CFR60.610(b)
P&G|AttachmentDTrinityConsultants 5
AirOxidationReactormeansanydeviceorprocessvesselinwhichoneormoreorganicreactantsarecombinedwithair,oracombinationofairandoxygen,toproduceoneormoreorganiccompounds.Ammoxidationandoxychlorinationreactionsareincludedinthisdefinition.ProcessUnitmeansequipmentassembledandconnectedbypipesorductstoproduce,asintermediatesorfinalproducts,oneormoreofthechemicalsin§60.617.Aprocessunitcanoperateindependentlyifsuppliedwithsufficientfuelorrawmaterialsandsufficientproductstoragefacilities.
TablerStationoperationsdonotincludeanairoxidationreactorasdefinedabove,nordotheyproduceachemicallistedin40CFR60.610.Therefore,P&Gdoesnotoperatean“affectedfacility”underNSPSIIIand,assuch,TablerStationisnotsubjecttotherequirementstherein.
NSPS RRR – SOCMI Reactors
Per40CFR60.700(a),NSPSRRRappliestoeachaffectedfacilitythatispartofaprocessunitthatproducesanyofthechemicalslistedin40CFR60.707asaproduct,co‐product,by‐product,orintermediate.Anaffectedfacilityisanyofthefollowingforwhichconstruction,modification,orreconstructioncommencedafterJune29,1990:5
> Eachreactorprocessnotdischargingitsventstreamintoarecoverystream;> Eachcombinationofareactorprocessandtherecoverysystemintowhichitsventstreamisdischarged;or> Eachcombinationoftwoormorereactorprocessesandthecommonrecoverysystemintowhichtheirvent
streamsaredischarged.
“Reactorprocesses”and“processunit”aredefinedin40CFR60.701asfollows:
Reactorprocessesareunitoperationsinwhichoneormorechemicals,orreactantsotherthanair,arecombinedordecomposedinsuchawaythattheirmolecularstructuresarealteredandoneormoreneworganiccompoundsareformed.
Processunitmeansequipmentassembledandconnectedbypipesorductstoproduce,asintermediatesorfinalproducts,oneormoreofthechemicalsin§60.707.Aprocessunitcanoperateindependentlyifsuppliedwithsufficientfeedorrawmaterialsandsufficientproductstoragefacilities.
TheTablerStationfacilitywillcontainareactorprocessconstructedafterJune29,1990.Therefore,thereactorprocessmeetsthedefinitionof“affectedfacility”underNSPSRRR.However,thisreactorprocessdoesnotproduceanyoftheaffectedchemicalslistedin40CFR60.707.Assuch,theP&GreactorprocessisnotsubjectNSPSRRR.
NSPS IIII – Stationary Compression Ignition Internal Combustion Engines
Thissubpartisapplicabletoownersandoperatorsofstationarycompressionignitioninternalcombustionengines(CIICE).TherewillbefiveCIICEonsite,threeforbackup/standbyuseonly(350kilowatt[kW])andtwofirepumpengines(311horsepower[hp]).Thebackup/standbygeneratorenginesaresubjecttotheemissionstandardsinTable1ofthesubpart,whilethefirepumpenginesaresubjecttoemissionstandardsinTable4ofthesubpart.Bothkindsofenginesarerequiredtouselow‐sulfurdiesel.Thebackup/standbygeneratorengineswillonlybeusedundermaintenanceconditionsorduringalossofpowertothesite;theywillhavealimitof100hoursperyear(each)foroperationinnon‐emergencysituations.Thehoursthebackup/standbygeneratorenginesareoperatedwillbetrackedwithanon‐resettablehourmeter.Recordkeepingandmonitoringrequirementsmayapplytothebackup/standbygeneratorenginesandthefirepumpengine.
540CFR60.700(b)
P&G|AttachmentDTrinityConsultants 6
NSPS JJJJ – Stationary Spark Ignition Internal Combustion Engines
Thissubpartisapplicabletoownersandoperatorsofstationarysparkignitioninternalcombustionengines(SIICE).TherewillbeoneSIICEonsiteforbackup/standbyuseonlywhichpowersa70kilowatt[kW]generator.Thebackup/standbygeneratorengineissubjecttotheemissionstandardsin40CFR1054.Thebackup/standbygeneratorenginewillonlybeusedundermaintenanceconditionsorduringalossofpowertothesite;itwillhavealimitof100hoursperyearforoperationinnon‐emergencysituations.Thehoursthebackup/standbygeneratorengineisoperatedwillbetrackedwithanon‐resettablehourmeter.Recordkeepingandmonitoringrequirementsmayapplytothebackup/standbygeneratorengine.
Non-Applicability of All Other NSPS
NSPSaredevelopedforparticularindustrialsourcecategories.AllotherNSPSarecategoricallynotapplicabletotheproposedchange.
National Emission Standards for Hazardous Air Pollutants (NEHSAP)
NationalEmissionsStandardsforHazardousAirPollutants(NESHAP),federalregulationsfoundinTitle40Part61and63oftheCFR,areemissionstandardsforHAP.NESHAPareapplicabletobothmajorsourcesofHAP(facilitiesthatexceedthemajorsourcethresholdsof10tpyofasingleHAPand25tpyofanycombinationofHAPfromstationarysources)aswellasnon‐majorsources(termed“areasources”).NESHAPapplytosourcesinspecificallyregulatedindustrialsourceclassifications(CleanAirActSection112(d))oronacase‐by‐casebasis(CleanAirActSection112(g))forfacilitiesnotregulatedasaspecificindustrialsourcetype.TheTablerStationfacilityisanareasourceofHAP.Assuch,thisdocumentonlyaddressesregulatoryapplicabilityforareasourcesanddoesnotincludeMACTstandardsformajorsources(e.g.,40CFRPart63SubpartFFFF,ortheMON).
NESHAP 4Z – Reciprocating Internal Combustion Engines
NESHAP4ZestablishesemissionlimitationsandoperatinglimitationsforHAPemittedfromstationaryreciprocatinginternalcombustionengines(RICE)locatedatmajorandareasourcesofHAP.Per40CFR6590(c)(1),newstationaryRICElocatedatanareasourcemayshowcompliancewithNESHAP4ZbybeingincompliancewithNSPS4IorNSPS4J.AllstationaryRICEP&GarenewandlocatedatanareasourceofHAPemissions.Therefore,bymaintainingcompliancewithNSPS4IorNSPS4J,P&GcandemonstratecompliancewithNESHAP4Z.
NESHAP 6J – Area Source Boilers
TheareasourceboilerNESHAPregulatesindustrial,commercial,andinstitutionalboilersthatburnsolidfossilfuel,biomass,orliquidfuel.ThefourboilersattheTablerStationfacilitywillburnnaturalgas.Per40CFR63.11237,alloftheboilersattheTablerStationfacilityqualifyasgas‐firedboilers.
Gaseousfuelsincludes,butisnotlimitedto,naturalgas,processgas,landfillgas,coalderivedgas,refinerygas,hydrogen,andbiogas.
Gas‐firedboilerincludesanyboilerthatburnsgaseousfuelsnotcombinedwithanysolidfuelsandburnsliquidfuelonlyduringperiodsofgascurtailment,gassupplyinterruption,startups,orperiodictestingonliquidfuel.Periodictestingofliquidfuelshallnotexceedacombinedtotalof48hoursduringanycalendaryear.
Gas‐firedboilersareexemptfromrequirementscontainedinthisregulation,per40CFR63.11195(e).Therefore,thefacilityisnotsubjecttoNESHAP6J.
P&G|AttachmentDTrinityConsultants 7
NESHAP 6V – Chemical Manufacturing Area Sources (CMAS)
Per40CFR63.11494(a),theCMASappliesachemicalmanufacturingprocessunit(CMPU)thatmeetsthefollowingcriteria:
> TheCMPUislocatedatanareasourceofHAPemissions;and> HAPlistedinTable1oftheCMASarepresentintheCMPUasfollows:
TheCMPUusesasfeedstock,anymaterialthatcontainsquinoline,manganese,and/ortrivalentchromiumatanindividualconcentrationgreaterthan1.0percentbyweight,oranyotherTable1HAPatanindividualconcentrationgreaterthan0.1percentbyweight.TodeterminetheTable1HAPcontentoffeedstocks,youmayrelyonformulationdataprovidedbythemanufacturerorsupplier,suchastheMaterialSafetyDataSheet(MSDS)forthematerial.IftheconcentrationinanMSDSispresentedasarange,usetheupperboundoftherange.
Quinolineisgeneratedasby‐productandispresentintheCMPUinanyliquidstream(processorwaste)ataconcentrationgreaterthan1.0percentbyweight.
Hydrazineand/orTable1organicHAPotherthanquinolinearegeneratedasby‐productandarepresentintheCMPUinanyliquidstream(processorwaste),continuousprocessvent,orbatchprocessventatanindividualconcentrationgreaterthan0.1percentbyweight.
HydrazineoranyTable1HAPisproducedasaproductoftheCMPU.
TheTablerStationfacilityisanareasourceofHAPemissions.However,therearenoTable1HAPspresentinanyoftheTablerStationfacilityoperations.Therefore,thefacilityisnotsubjecttotheCMAS.
NESHAP 7B – Chemical Preparations Area Sources
Per40CFR63.11579(a),NESHAP7Bappliesifallofthefollowingconditionsaremet:
> Operateachemicalpreparationsfacility;> ThechemicalpreparationsfacilityisastationaryareasourceofHAP;and> ThechemicalpreparationsfacilityhasatleastonechemicalpreparationsoperationintargetHAPservice.
“IntargetHAPservice”isdefinedunder40CFR63.11588asfollows:
IntargetHAPservicemeansthatequipmentinthechemicalpreparationoperationeithercontains,contacts,orisprocessingtargetHAP‐containingmaterials.
Additionally,“targetHAP”aredefinedasmetalcompoundsforchromium,lead,manganese,andnickel.TheTablerStationfacilitydoesnothaveachemicalpreparationoperationthatcontains,contacts,orprocessesanymetalcompoundsforchromium,lead,manganese,and/ornickel.Therefore,theTablerStationfacilityisnotsubjecttoNESHAP7B.
Non-Applicability of All Other NESHAP
SimilartoNSPS,NESHAParedevelopedforparticularindustrialsourcecategories.AllotherNESHAParecategoricallynotapplicabletotheproposedchange.
P&G|AttachmentDTrinityConsultants 8
West Virginia SIP Regulations
TheproposedprojectattheTablerStationfacilityispotentiallysubjecttoregulationscontainedintheWestVirginiaCodeofStateRegulations,Chapter45(CodeofStateRegulations).WestVirginiaregulationspotentiallyapplicabletotheproposedprojectarediscussedbelow.
45 CSR 2: Particulate Air Pollution from Combustion of Fuel in Indirect Heat Exchangers
45CSR2appliestofuelburningunits,definedasequipmentburningfuel“fortheprimarypurposeofproducingheatorpowerbyindirectheattransfer”.TheboilersattheTablerStationfacilitymeetsthisdefinitionandarethereforesubjectto45CSR2.Per45CSR2‐3,opacityofemissionsfromtheboilersshallnotexceed10percentarebasedonasixminuteblockaverage.Per45CSR2‐4,theparticulateemissionslimitforType‘b’fuelburningunits6istheproductof0.09andthetotaldesignheatinput(62MMBtu/hrand31MMBtu/hr),whichis5.58poundsperhour(lb/hr)and2.79lb/hr,respectively.
45 CSR 4: To Prevent Objectionable Odors
45CSR4‐2.01specifiesthat:
Nopersonshallcause,suffer,alloworpermitthedischargeofairpollutantswhichcauseorcontributetoanobjectionableodoratanylocationoccupiedbythepublic.
P&Gtakesprecautionstoassurecompliancewiththisrule.Accidentalorotherinfrequentemissionsofodorarenotprovisionsofthisrule.Thisregulationisnotfederallyenforceable.
45 CSR 6: To Prevent and Control Air Pollution from Combustion of Refuse
45CSR6setsforthrequirementsforlimitingemissionsfromincinerationwhichisdefinedas“thedestructionofcombustiblerefusebyburninginafurnacedesignedforthatpurpose.Forthepurposesofthisrule,thedestructionofanycombustibleliquidorgaseousmaterialbyburninginaflareorflarestack,thermaloxidizer,orthermalcatalyticoxidizerstackshallbeconsideredincineration.”Theproposedregenerativethermaloxidizermeetsthisdefinitionandisthereforesubjecttothisregulation.TheregenerativethermaloxidizerwillbesubjecttothePMemissionlimitsin45CSR6‐4.1.Inaddition,opacityfromtheregenerativethermaloxidizerwillbelimitedto20%per45CSR6‐4.3exceptasprovidedin45CFR6‐4.4.
45 CSR 7: To Prevent and Control Particulate Matter from Manufacturing Processes
45CSR7regulatesPMemissionsfrommanufacturingprocessesandassociatedoperations.45CSR7‐3,requiresa20%opacitylimitfromallprocesssourceoperations.Section45CSR7‐4andTable45‐7Asetparticulateemissionslimitsbasedonthetotalweightofallmaterialsusedbythefacility,alsoknownastheprocessweight.ThedifferentprocessareasattheTablerStationfacilityqualifyunderdifferentclassificationsaspartoftherule.Thesurfactantsareaisamineralacidproducingarea,7subjecttolimitsinTable45‐7B.Theliquidsoap,dryconsumerlaundryandcleaningproducts,andplasticsmoldingareasqualifyasType‘a’facilities.8Theutilitiesareaiscoveredunder45CSR2,andisexemptfromthisrule,accordingto45CSR5‐10.1.ThemaximumallowabletotalstackemissionrateforeachareaareshowninTableD‐1.
6Per40CSR2‐10(b):“Type'b'meansanyfuelburningunitnotclassifiedasaType'a'orType'c'unitsuchasindustrialpulverized‐fuel‐firedfurnaces,cyclonefurnaces,gas‐firedandliquid‐fuel‐firedunits.”7Themineralacid,sulfuricacid,isanincidentalbyproductofsurfactantmanufacturing.8Per45CSR7‐2.39(a),“Type‘a’meansanymanufacturingprocesssourceoperationinvolvingglassmelting,calcination,orphysicalchangeexceptasnotedintype‘c’below.”(emphasisadded)
P&G|AttachmentDTrinityConsultants 9
TableD‐1.ProcessWeightRuleLimits
ProcessArea ProcessWeightRate MaxStackEmissionRate
Surfactants “MineralAcid”–Table45‐7B 35mg/m3
LiquidSoapAandB >600,000lb/hr 50lb/hr
DryConsumerLaundryandCleaningProducts
>600,000lb/hr 50lb/hr
PlasticsMaking >20,000lb/hr 16mg/m3
Utilities Exempt‐CoveredUnder45CSR2
PlasticsMakingUtilities Exempt‐CoveredUnder45CSR2
45 CSR 10: To Prevent and Control Air Pollution from the Emission of Sulfur Oxides
45CSR10appliestofuelburningunits,definedasequipmentburningfuel“fortheprimarypurposeofproducingheatorpowerbyindirectheattransfer”.TheboilersattheTablerStationfacilitymeetsthisdefinitionandisthereforesubjectto45CSR10.SinceBerkeleyCountyisinaPriorityIIIregion,per45CSR10‐3.1(e),thesulfurdioxideweightemissionsstandardistheproductof3.2andthetotaldesignheatinput(166MMBtu/hr),or531lb/hr.
45 CSR 16: Standards of Performance for New Stationary Sources
Thisruleadoptsthestandardsofperformancefornewstationarysourcessetforthin40CFRPart60byreference.PotentiallyapplicableNSPSarediscussedabove.
45 CSR 21: To Prevent and Control Air Pollution from the Emission of Volatile Organic Compounds
45CSR21isintendedtorequirereasonablyavailablecontroltechnologyforVOCsourcesinPutnam,Kanawha,Cabell,Wayne,andWoodCounties.Assuch,theserequirementsdonotapplytoVOCsourcesinBerkeleyCounty.
45 CSR 27: To Prevent and Control the Emissions of Toxic Air Pollutants
WestVirginiaregulatestheemissionsoftoxicairpollutantemissionsthrough45CSR27.Afacilitythatdischarges,ormaydischarge,atoxicpollutantintotheopenatmosphereinquantitiesgreaterthanthosedelineatedinTableAofthisruleisrequiredtoemployBestAvailableTechnology(BAT)onallchemicalprocessingequipmentemittingthepollutant.TheequipmentattheTablerStationfacilitydischargestraceamountsofbenzeneandformaldehydeduringnaturalgascombustion.However,theTablerStationfacilitydoesnotdischargebenzeneandformaldehydeinaquantitygreaterthanlistedinTableA,asshowninTableD‐2.Assuch,thisregulationdoesnotapplytotheprojectattheTablerStationfacility.
P&G|AttachmentDTrinityConsultants 10
TableD‐2.EvaluationofToxicAirPollutants
Pollutant1 45CSR27EmissionRate
Threshold1(lb/yr)TablerStationEmission
Rate(lb/yr)Is45CSR27Applicable?
Acrylonitrile 500 0 NoAllylChloride 10,000 0 NoBenzene 1,000 <1 No
1,3Butadiene 500 0 NoCarbonTetrachloride 1,000 0 No
Chloroform 1,000 0 NoEthyleneDichloride 1,000 0 NoEthyleneOxide 500 0 NoFormaldehyde 1,000 <1 No
MethyleneChloride 5,000 0 NoPropyleneOxide 5,000 0 NoTrichloroethylene 10,000 0 NoVinylChloride 1,000 0 No
VinylideneChloride 2,000 0 No1From40CSR27,TableA
45 CSR 31 Confidential Information
45CSR31describestherequirementsforclaimingconfidentialinformation,andtheproceduresfordeterminationsofconfidentiality.ConfidentialitymaybeclaimediftheDirectordeterminesthatthefacilitymeetsthecriteriadetailedin45CSR31‐4.1(a‐e).P&GhasdeterminedthattheTablerStationR‐13applicationdoesnotmeetthecriteriaforconfidentialsubmittal.
45 CSR 34: Emission Standards for Hazardous Air Pollutants
ThisruleadoptstheNationalEmissionsStandardsforHazardousAirPollutants(NESHAPs)byreference.PotentiallyapplicableNESHAParediscussedabove.
P&G – Tabler Station | R13 Permit Trinity Consultants
ATTACHMENT E
Plot Plan
C4
C3
C5
INTERSTATE 81(VARIABLE WIDTH)
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INTERSTATE 81(VARIABLE WIDTH)
INTERSTATE 81(VARIABLE WIDTH)
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INTERSTATE 81(VARIABLE WIDTH)
15' BUILDING SETBACK
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75' BUILDING SETBACK
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75' BUILDING SETBACK
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L35
L33
L31
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L27
L26
L23
N 36°12'10" E 769.27'
N 04°07'56" W
361.48'
S 67°0 9
'38" E 12
73.64 ' (TO
TAL)
S 16°43'52" W 2659.34'
L21
L22
L19
C1
L18L17
L15
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L9L8
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N 04°19'02" W
613.84'
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L16
L10
L12
L7
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L1
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N/F GILBERT S. &LINDA K. BARNEYDB. 355 PG. 733TAX MAP A14
PARCEL 9USE: RESIDENTIAL
N/F PHILIP A. &BETTY M. BARNEY
DB. 378 PG. 81TAX MAP A14PARCEL 9.7
N/F PHILIP A. &BETTY M. BARNEY
DB. 378 PG. 79TAX MAP A14PARCEL 9.6
N/F STEVE &BONITA B. BEALDB. 378 PG. 77TAX MAP A14PARCEL 9.4
PARCEL BBERKELEY COUNTY
DEVELOPMENT AUTHORITYTAX MAP A10 PARCEL 1.2
45.0180 ACRES(ADJUSTED)
USE: VACANT
N/F ALLMINE PAVING LLCDB. 952 PG. 642P.C. 15, SL. 28
TAX MAP A15 PARCEL 32USE: COMMERCIAL
N/FA&S WAREHOUSE INC.
DB. 777 PG. 376TAX MAP 14-12
DB. 508 P
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N/F STEVE &BONITA B. BEALDB. 355 PG. 730TAX MAP A14PARCEL 9.3
BERKELEY COUNTYDEVELOPMENT AUTHORITY
TAX MAP A15 PARCEL 2"WEST PORTION"
10.6925 ACRES(ADJUSTED)
BER
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PM
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CRESTFIELD SUBDIVISION
N/F CLARENCE LEE RIDGELYDB. 483 PG. 188
TAX MAP A10 PARCEL 116.1USE: COMMERCIAL
N/F JAMES P. & SHARON A. GARVINDB. 420 PG. 569
TAX MAP A10 PARCEL 4USE: RESIDENTIAL
N/F
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WINCHESTER & WESTERN RAILROAD ( DB. 409 PG. 125)
PARCEL BBERKELEY COUNTY
DEVELOPMENT AUTHORITYTAX MAP A10 PARCEL 1.2
LOT
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DB. 241 PG
. 118
DB. 436 PG
. 690
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SANITARY SEWER ESMT.P.C. 14 SL. 104P.C. 15 SL. 28P.C. 112-124
75' BUFFER YARD
25' BUFFER YARD
5' BUFFER YARD
25' BU
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DEVELOPMENT AUTHORITYTAX MAP A10 PARCEL 1.4
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N/FY SCOTT AND WRIGHT-MILLER JUDITH L.
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N/F
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DEVELOPMENT DRIVEPRIVATE RIGHT-OF-WAY
P.C. 14, SL. 104-110
DEVELOPMENT DRIVEPRIVATE RIGHT-OF-WAY
P.C. 14, SL. 104-110
BERKELEY COUNTY DEVELOPMENT AUTHORITY"WEST PORTION"DB. 754 PG. 123
TAX MAP A15 PARCEL 2USE: VACANT
BERKELEY COUNTYDEVELOPMENT AUTHORITY
DB. 1026 PG. 26TAX MAP A10 PARCEL 1.3
USE: VACANT
WINCHESTER & WESTERN RAILROAD ( DB. 409 PG. 125)
"UNECONOMIC REMNANT" NOTED ON RIGHT OF WAY
PLANS FOR STATE PROJECTNO. X302-81/8-0.00 00
LOT
24 SEC
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LOT
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BERKELEY COUNTY DEVELOPMENT AUTHORITY"WEST PORTION"DB. 754 PG. 123
TAX MAP A15 PARCEL 2
WATERLINE ESMT.P.C. 14 SL. 104P.C. 15 SL. 28P.C. 112-124
SANITARY SEWER ESMT.P.C. 14 SL. 104P.C. 15 SL. 28P.C. 112-124
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POWER LINES & POLES COVEREDBY RIGHT-OF-WAY AGREEMENT WITH
POTOMAC EDISON CO. OF WV.DB. 238 PG. 531
PC. 14 SL. 47
75' BUFFER YARD
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100' B
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50' SETBACKFROM WWRR
25' BUFFER YARD
UDITH L.
N/F JAMES P. & SHARON A. GARVINDB. 420 PG. 569
TAX MAP A10 PARCEL 4USE: RESIDENTIAL
100' BUFFER YARD
TANK
TEMPORARY STAGE ICONTRACTOR YARD
FUTURE BUILDING
PROPOSEDRELOCATED
CELLTOWER
LOCATION
TRAILER DROP 250 SPACES
FUELING(INTERNAL USE ONLY)
PHASE 2 CONSTRUCTION FACILITIES
PROP ACCESS ROADBY WVDOH
80' ROWADT = 2480 VPD
VEHICULAR ACCESS
RAIL YARD
PHASE 2BUILDING
CONSTRUCTIONOPERATIONS
CONSTRUCTIO
N OPERATIO
N ACCESS
RAIL YARD
PHASE ICONTRACTOR
PARKING396
SPACES(REMOVED IN
PHASE II)
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PROP TRUCK
ENTRANCE ROAD
BY WVDOH
80' ROW
ADT=530 VPD
WAITINGAREA
GUARDHOUSE
TRUCKSCALES
END OFPUBLICACCESS
END OFPUBLICACCESS
GUARDHOUSE
PROP ROUNDABOUTEND OF PUBLIC
ACCESS
PROPOSEDSIDEWALK
EMERGENCYACCESS
PONDACCESSROAD
EXISTING MARTHA DRIVETO BE VACATED BEYOND
WWRR ROW
PROPOSED ACCESS BYWVDOH TO ROUTE 11ENTRANCE TRIP GENERATIONESTIMATED AT 1120 VPD
EXISTING STEWART AVE.TO BE VACATED BEYONDWWRR ROW
PHASE I PARKING427 SPACES
PHASE I PARKING35 SPACES
PHASE I PARKING19 SPACES
COURTYARD DECK
EN
TR
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24 X 60
24 X 60
24 X 60
8 X
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8 X
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GUARDSHACK
STAIR
S STAIR
S LIGHT
LIGHT
ROUTE 11CONNECTORBY WVDOH
PROPOSED 10'ELECTRIC ESMT
PROPOSED 50'ELECTRIC ESMT
PROPOSED 50'ELECTRIC ESMT
PROPOSED 50'ELECTRIC ESMT
SCALE
TAIL TRACK
CANOPY
CANOPY
POINT OFCONNECTION
POINT OFCONNECTION
MS-1A
MS-1A
PROPOSEDSIDEWALK
PROPOSEDSIDEWALK
PROPOSEDSIDEWALK
PHASE 2 CONSTRUCTION FACILITIES
PHASE I PARKING978 SPACES
CLASS 3A CONCRETEJACK PAD (TYP.)
CLASS 3A CONCRETEJACK PAD (TYP.)
CLASS 3A CONCRETEJACK PAD (TYP.)
POND ACCESS ROAD
PONDACCESSROAD
PHASE II TRAILER DROP LOT (444 SAPCES)
PROPOSEDCROSSWALK
SIGN (TYP)
PROPSTOPSIGN(TYP)
PROP STOPSIGN (TYP)
PROPSTOPSIGN(TYP)
PROPSTOPSIGN(TYP)
PROP STOPSIGN (TYP)
CG-12A
PROPOSEDWVDOH ROW
MS-1A
PROP 10' SIDEWALK
FUTURE ROAD
FUTURE BUILDING
PR
OP
10'
SID
EW
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ROCK CRUSHINGOPERATIONS
BATCH PLANTOPERATIONS
ROCK CRUSHINGOPERATIONS
ROCK CRUSHINGOPERATIONS
ROCK CRUSHINGOPERATIONS
FU
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FUTURE PARKING
LIMITS OF TEMPORARYSTOCKPILE AREA
LIMITS OF TEMPORARYSTOCKPILE AREA
LIMITS OF TEMPORARYSTOCKPILE AREA
LIMITS OF TEMPORARYSTOCKPILE AREA
24 X 60
24 X 60
PROP 20' WL ESMT
PROP 20' WL ESMT
5 30
PROCESS WASTEWATER TANK FARM
FUTURE
FUTURE
FUTURE
P&G – Tabler Station | R13 Permit Trinity Consultants
ATTACHMENT F
Detailed Process Flow Diagram
Process Flow Diagram F-1: General Process
October 2016141801.0078
P&G Tabler Station WV
Utilities
Raw Materials
Surfactant Making Liquid Soap
Consumer Products (Mixing and Filling)
Dry Consumer Laundry and
Cleaning Products (Mixing and Coating)
Shipping
Plastics Molding
Plastics Molding Utilities
Neutralization Process
Finished Product Handling, Storage
and Transfer
For Onsite and Offsite Use
Raw MaterialUnloading Raw Materials
Handling, Storage and Transfer
Surfactant Making Process
Process Flow Diagram F-2: Surfactants Process
P&G Tabler Station WV
October 2016
Prepared by:Project: 141801.0078
During Startup/ShutdownChangeover
Sulfur Trioxide Absorber
Incidental By Product:
Sulfuric Acid Handling, Storage,
and Transfer
Incidental By Product: Precipitated
Acid Mix Handling, Storage, and Transfer
Sulfuric Acid and PAM Loading
Legend
Emissions
Process Flow
Sulfur Dioxide Scrubber
Fugitive
Fugitive
Fugitive
Process Flow Diagram F-3: Liquid Soap A and B Making
Process
October 2016141801.0078
P&G – WV Tabler Station
Process Flow
Legend
Air Emissions Rotoclone
Thermal Oxidizer
Bulk Material Unloading
Bulk Liquid Storage, Handling &
Transfer
Tote and Drum Unloading
Dry Unloading
Liquid Soap A Mix Tanks
Finished Product Warehouse
Finished Product Shipping
Packaging Lines
Packaging Supply
Surfactant Process Tank
Surfactants
Finished Product Tanks
Central Preweigh
From
Che
mica
ls Ar
ea
Tank
Far
ms
H2O
During Volatile Material Use
H2O
Day Process Tanks
Liquid Soap B Mix Tanks
H2O
Liquid Soap Making Process
Wastewater Flow
FugitiveFugitive
Fugitive
Fugitive
Fugitive
Fugitive
Fugitive
Process Flow Diagram F-4: Simple Dry Consumer Products A
P&G – Tabler Station WV
Solid Material Unloading
Liquids Unloading
Raw Material Addition and Preparation for
Packaging
Packaging
Process Flow
Legend
Emissions Baghouse
Solid Material Storage, Handling & Transfer Intermediate Mixing
Liquids Storage, Handling & Transfer
Packaging Supply
Finished Product to Warehouse and Shipping
Substrate
October 2016
Prepared by:Project: 141801.0078Filter
Fugitive
Fugitive
Tote and Drum UnloadingDay
Process Tanks
Fugitive
Process Flow Diagram F-5: Utilities
October 2016141801.0078
P&G – WV Tabler Station
Engine ULSD Tanks
(<500 gallon)
Vehicle Refueling
ULSD Tank(5,000 gallons)
Boilers (2) – 62 MMBtu/hr, eachBoiler (1) – 31 MMBtu/hr
Temp Boiler (1) – 11 MMBtu/hr
Cooling Towers (3) – 5,117 gallons/min
13,200 gallons/min3,533 gallons/min
Fire Pump Engine311 hp
Fire Pump Engine311 hp
Backup/Standby
Generator350 kW
Backup/Standby
Generator350 kW
Backup/Standby
Generator350 kW
Warehouse Heating
14-20 MMBtu/hr (total)
TEMP
Water PretreatmentWastewater Pretreatment
Emissions
Fugitive
Fugitive
Fugitive
Fugitive
Fugitive Fugitive Fugitive
Legend
Process Flow Diagram F-6: Plastics Molding Supplier
October 2016141801.0078
P&G – WV Tabler Station
Cooling Tower
Backup/Standby
Generator
Surge BinsStorage Silos
Pressing and Molding
OperationsTransport to
Production Area
Process Flow
Legend
EmissionsCyclone
Space Heating
Parts Washing
Railcar Unloading
Fugitive
General Process Cleaning
Plastic Regrind
P&G – Tabler Station | R13 Permit Trinity Consultants
ATTACHMENT G
Process Description
P&G|AttachmentGTrinityConsultants 1
ATTACHMENT G – PROCESS DESCRIPTION
Aspartofthisproject,P&Gproposestoinstallequipmentinthefollowingdifferentbusinessareas:> SurfactantManufacturing;> LiquidSoapMakingAandB;> DryConsumerProductsA;> PlasticsMolding;and> Utilities.Eachofthesebusinessareasarediscussedingreaterdetailinthereport.
P&G – Tabler Station | R13 Permit Trinity Consultants
ATTACHMENT H
Materials Safety Data Sheets
Attachment HTabler Station
TablerStationSiteMaterialListing
MaterialNameProcessAreas18MMSiliconeALSAMTriquatAmodimethicone(10TAS)AXSBeautyCare(HairCare,BodyWash)Perfumes(multiple)BeautyCareFinishedProducts(multiple)BentoniteClayBenzylAlcoholBetaineBetzdearbornIEC2C24AE1AlcoholEthoxylateC24AE3AlcoholEthoxylateCaustic,50%CetylAlcoholCO1214CorrshieldMD4103CuttingOilThreadCuttingLubricantDADMACDC‐1865DC‐1872DCMCDiethyleneglycol(heattransferfluid)Dimethicone(10,000cSt)Dimethicone(15‐85)DM5500PolydimethylSiloxaneEmulsionEDDSEjectorPinEthanol,denaturedFattyAcidFlogardPOT6183FoodGradeSiliconeFormoleneHB5502FFormoleneHighDensityPolyethylene‐HexaneCopolymerGengardGN7112GlycerinGlydantHydrochloricAcidHydroForceFoamingCitrusAllPurposeCleanerIMSPaintableMistInhibitorAZ8101KathonKRALaureth‐4L‐GlutamicAcidLinoleMarlexKN226PolyethyleneMarlexKN226PolyethyleneMiramod‐BulkPerfumeNalco1720Nalco1820Nalco3DT265
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Attachment HTabler Station
TablerStationSiteMaterialListing
MaterialNameNalco7320Nalco7330NalcoNexguard22310NeolonePanthenolPantylPerfumeMicroCapsulesPerfumes(multiple)PetrolatumPhenoxyethanolPolyethyleneResinPolypropyleneHomopolymerPolyquaterium‐10PQASPrecipatedAcidMix(PAM)PropyleneGlycol(heattransferfluid)S2TSSteolTD402‐65SAPDMASimpleGreenAll‐PurposeCleanerSlideMoldCleanerPlusDegreaser4SlideMoldShieldCylinderSlideResinRemoverAerosolSlideSuperGreaseSodiumHypochloriteSolutionSodiumLaurethSulfateSLE1SSodiumLaurethSulfateSLE3SSodiumLaurylSulfateSLSSpectrusNX1100StearylAlcoholStepTwoRustStopperSulfuricAcidSuperGreaseAerosolSXSTDA‐3UltimateUV390‐1UltraLowSulfurDieselFuelWhiteSilver‐3
LabChemicals(Deminimis)0.01NHydrochloricAcid0.01NIodineSolution0.01NSodiumHydroxide0.01NSodiumThiosulfate0.025MSodiumSulfate0.04NIodineSolution0.04NIodineSolution0.05NSodiumHydroxide0.1NEDTADisodiumSalt0.1NHydrochloricAcid0.1NHydrochloricAcidinIPA0.1NIodineSolution0.1NPerchloricAcidinAceticAcid0.1NSilverNitrate
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141801.0078
Attachment HTabler Station
TablerStationSiteMaterialListing
MaterialName0.1NSodiumHydroxide0.1NSodiumThiosulfate0.1NSulfuricAcid0.25NSodiumHydroxide0.2MHydrochloricAcid0.5NHydrochloricAcid0.5NPotassiumHydroxide1%HydrochloricAcid1,3‐dioxane1,3‐Butanediol(butyleneglycol)1,4‐dioxane10%SodiumHydroxide1000mg/LFestandard1000ppmIronindiluteacid1‐Chlorodocosane(C22‐Cl)1‐Chloroeicosane(C20‐Cl)1‐Chlorohexadecane1‐Chlorooctadecane1‐Docosanol1‐Dodecanol1‐Eicosanol1‐Hexadecanol1NHydrochloricAcid1NSodiumHydroxide1NSulfuricAcid1‐Nonadecanol1‐Octadecanol1‐Pentadecanol1‐Tetracosanol1‐Tetradecanol25%ActiveAE3S28‐30%StrongAmmoniaSolution2‐Phenoxyethanol37%FormaldehydeSolution50%SodiumHydroxide6mLx1000mgSAXSPEcartridge7.5%HydrogenPeroxide90%LA‐7AEAbsoluteEthanolAcc‐FluorReagentKitAceticAcidAceticAcid(HPLCGrade)AcetoneAcetonitrile(HPLCGrade)AcetylacetoneAcetyleneGasAE3SAmberliteMB‐1IonExchangeResinAmmoniumAcetateAmmoniumChlorideAmmoniumHydroxideAmmoniumXyleneSulphonateAquamerckFormaldydeTestKit(0.1ppm)
3 of 6Trinity Consultants
141801.0078
Attachment HTabler Station
TablerStationSiteMaterialListing
MaterialNameBenzoicAcidBenzylAlcoholBenzylaldehydeBF3/MethanolBromocresolGreenIndicatorBromothymolBlueIndicatorButan‐2‐olButylAlcoholButylParabenCaffeine,anhydrousCalciumChlorideDihydateCalibrationStdCanonOilStandardN140CanonOilStandardN250ChloroformChromotropicAcidCitricAcidMonohydrateComposite5VolumetricCoulomatAGD6CylcomethiconeDecamethylpentasiloxane(D5Cyclomethicone)DecanoicAcidDiethyleneGlycolDiethyleneGlycolDimidiumBromideDiphenyloxideDipropyleneGlycolDishwashingDetergentDisodiumDihydrogenEthyleneDiamineTetraAcetateDihydrateDisodiumHydrogenPhosphateAnhydrousDisodiumHydrogenPhosphateHeptahydrateDisperseRed17ReferenceStdDisulfineBlueVNDNPHDodecanolD‐PanthenolD‐PanthenylEthylEtherDryMethanolEicosanoicAcidElaidicAcidElectrodeReferenceSolutionEriochromeBlackErythorbicAcidEthoxylatedAlcoholEthyleneGlycolEthyleneGlycolEthyleneGlycolDistearateFerricAmmoniumSulfateFerricChlorideHexahydrateFerroVerIronReagentPowderPillowsFIDCheckSampleFilterPaperFinishedPerfumeOil
4 of 6Trinity Consultants
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Attachment HTabler Station
TablerStationSiteMaterialListing
MaterialNameFlavorStandardFluorenoneFormicAcidGlycerinGlycineHeptadecanoicAcidHexadecanolHexadecylHexadecanoateHexamethyltrisiloxane(D3Cyclomethicone)HexaneHyamine1622HydrochloricAcidHydrogenPeroxide(30%)HydroxylamineHydrochlorideIodineIPBCStandardIsooctaneIsopropylAlcoholKathonCG/ICPII®(CG/ICPII)StandardLauricAcidLaurinaldehydeLeadNitrateLinoleicAcidMerckoquantFormaldehydeTestKit(10ppm)MethanolMethanol(HPLCGrade)MethylIsobutylKetoneMethylOrangeIndicatorSolutionMethylParabenMethylRedIndicatorMethyleneChlorideMethyleneChloride(HPLCGrade)MineralOil,NujolMyristicAcidN,N‐Dimethyl‐n‐hexadecylamine(C16DMA)N,N‐Dimethyl‐n‐octadecylamine(C18DMA)NeoloneRMn‐HeptaneNicotinamideNitricAcidNitrousOxideGasn‐Pentacosanen‐TricosaneOctamethyltetrasiloxane(D4Cyclomethicone)OctanoicAcidOleicAcido‐PhenanthrolinePalmiticAcidPalmitoleicAcidPapersamplecupswithlidsPentadecanolPerfumeBlottersPerfumeMaterialStandard
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Attachment HTabler Station
TablerStationSiteMaterialListing
MaterialNamePerfumeRawMaterialsPetrolatumPetroleumEtherpH10BufferpH4BufferpH7BufferPhenolphthaleinSolutionPhosphateSpectroquantKitPhosphoricAcidPhosphoricAcid(HPLCGrade)Plasticsamplecupswithlidsp‐Nitrophenol,indicatorPotassiumBiphthalatePotassiumBromidePowderPotassiumChloratePotassiumChromateIndicatorPotassiumDihydrogenPhosphatePotassiumhexacyanoferrate(II)Potassiumhexacyanoferrate(III)PotassiumHydrogenPhthalatePotassiumHydroxide(pellets)PotassiumIodidePropylParabenSalicylAlcoholsiliconeanti‐foamSodiumChlorideSodiumDihydrogenPhosphateMonohydrateSodiumLaurylSulfateSodiumSulfateSodiumThiosulfateSPBrandMICROSqualaneStarchIndicatorStearicAcidSulfuricAcidSulfuricAcid(<0.1ppmChloride)SylonBFTTargetAppearanceStdTargetOdorStandardsTetradecanolTetrahydrofuranTolueneTridecanoicAcidTridecanolTrisodiumCitrateDihydrateTritonX‐100TrizmaBaseWaterStandard
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P&G – Tabler Station | R13 Permit Trinity Consultants
ATTACHMENT I
Emission Units Table
Attachment ITabler Station
EmissionUnitID1
EmissionPointID2
EmissionUnitDescriptionYear
Installed/Modified
DesignCapacityType3anddateofChange
ControlDevice4
1S 1E SurfactantMakingProcess 2017 3,000gal/hr New 1C
2S 2E SurfactantMakingProcess 2017 3,000gal/hr New 2C
3S 3E SurfactantTanks 2017 120,762gal New ‐‐4S 4E SurfactantTanks 2017 48,345gal New ‐‐5S 5E SurfactantTanks 2017 40,109gal New ‐‐6S 6E SurfactantTanks 2017 40,109gal New ‐‐7S 7E SurfactantTanks 2017 15,125gal New ‐‐8S 8E SurfactantTanks 2017 15,125gal New ‐‐9S 9E SurfactantTanks 2017 15,125gal New ‐‐10S 10E SurfactantTanks 2017 72,475gal New ‐‐11S 11E SurfactantTanks 2017 72,475gal New ‐‐12S 12E SurfactantTanks 2017 72,475gal New ‐‐13S 13E SurfactantTanks 2017 72,475gal New ‐‐14S 14E SurfactantTanks 2017 72,475gal New ‐‐15S 15E SurfactantTanks 2017 72,475gal New ‐‐16S 16E SurfactantTanks 2017 26,083gal New ‐‐17S 17E SurfactantTanks 2017 15,125gal New ‐‐18S 18E SurfactantTanks 2017 15,125gal New ‐‐19S 19E SurfactantBulkLiquidTransfer 2017 17,150,000gal/yr New ‐‐20S 20E LiquidSoapAandBTanks 2017 39,626gal New ‐‐21S 21E LiquidSoapAandBTanks 2017 39,626gal New ‐‐22S 22E LiquidSoapAandBTanks 2017 39,626gal New ‐‐23S 23E LiquidSoapAandBTanks 2017 7,925gal New ‐‐24S 24E LiquidSoapAandBTanks 2017 7,925gal New ‐‐25S 25E LiquidSoapAandBTanks 2017 39,626gal New ‐‐26S 26E LiquidSoapAandBTanks 2017 15,850gal New ‐‐27S 27E LiquidSoapAandBTanks 2017 39,626gal New ‐‐28S 28E LiquidSoapAandBTanks 2017 26,417gal New ‐‐29S 29E LiquidSoapAandBTanks 2017 15,850gal New ‐‐30S 30E LiquidSoapAandBTanks 2017 26,417gal New ‐‐31S 31E LiquidSoapAandBTanks 2017 15,850gal New ‐‐32S 32E LiquidSoapAandBTanks 2017 15,850gal New ‐‐33S 33E LiquidSoapAandBTanks 2017 7,925gal New ‐‐34S 34E LiquidSoapAandBTanks 2017 7,925gal New ‐‐35S 35E LiquidSoapAandBTanks 2017 7,925gal New ‐‐36S 36E LiquidSoapAandBTanks 2017 7,925gal New ‐‐37S 37E LiquidSoapAandBTanks 2017 7,925gal New ‐‐50S 50E LiquidSoapAandBTanks 2017 7,925gal New ‐‐56S 56E LiquidSoapAandBTanks 2017 7,275gal New ‐‐53S 53E LiquidSoapAandBTanks 2017 7,925gal New ‐‐38S 38E LiquidSoapAandBTanks 2017 396gal New ‐‐40S 40E LiquidSoapAandBTanks 2017 396gal New ‐‐41S 41E LiquidSoapAandBTanks 2017 396gal New ‐‐42S 42E LiquidSoapAandBTanks 2017 396gal New ‐‐43S 43E LiquidSoapAandBTanks 2017 396gal New ‐‐44S 44E LiquidSoapAandBTanks 2017 396gal New ‐‐45S 45E LiquidSoapAandBTanks 2017 396gal New ‐‐46S 46E LiquidSoapAandBTanks 2017 396gal New ‐‐47S 47E LiquidSoapAandBTanks 2017 396gal New ‐‐51S 51E LiquidSoapAandBTanks 2017 396gal New ‐‐52S 52E LiquidSoapAandBTanks 2017 396gal New ‐‐54S 54E LiquidSoapAandBTanks 2017 660gal New ‐‐55S 55E LiquidSoapAandBTanks 2017 396gal New ‐‐57S 57E LiquidSoapAandBTanks 2017 1,057gal New ‐‐59S 59E LiquidSoapAandBTanks 2017 396gal New ‐‐60S 60E LiquidSoapAandBTanks 2017 132gal New ‐‐61S 61E LiquidSoapAandBTanks 2017 396gal New ‐‐63S 63E LiquidSoapAandBTanks 2017 396gal New ‐‐64S 64E LiquidSoapAandBTanks 2017 396gal New ‐‐65S 65E LiquidSoapAandBTanks 2017 396gal New ‐‐66S 66E LiquidSoapAandBTanks 2017 396gal New ‐‐67S 67E LiquidSoapAandBTanks 2017 396gal New ‐‐68S 68E LiquidSoapAandBTanks 2017 396gal New ‐‐69S 69E LiquidSoapAandBTanks 2017 396gal New ‐‐70S 70E LiquidSoapAandBTanks 2017 396gal New ‐‐71S 71E LiquidSoapAandBTanks 2017 396gal New ‐‐72S 72E LiquidSoapAandBTanks 2017 396gal New ‐‐73S 73E LiquidSoapAandBTanks 2017 396gal New ‐‐74S 74E LiquidSoapAandBTanks 2017 396gal New ‐‐75S 75E LiquidSoapAandBTanks 2017 396gal New ‐‐76S 76E LiquidSoapAandBTanks 2017 396gal New ‐‐77S 77E LiquidSoapAandBTanks 2017 396gal New ‐‐87S 87E LiquidSoapAandBTanks 2017 1,585gal New ‐‐88S 88E LiquidSoapAandBTanks 2017 1,585gal New ‐‐89S 89E LiquidSoapAandBTanks 2017 1,585gal New ‐‐90S 90E LiquidSoapAandBTanks 2017 1,585gal New ‐‐91S 91E LiquidSoapAandBTanks 2017 1,585gal New ‐‐92S 92E LiquidSoapAandBTanks 2017 1,585gal New ‐‐93S 93E LiquidSoapAandBTanks 2017 1,585gal New ‐‐94S 94E LiquidSoapAandBTanks 2017 1,585gal New ‐‐94bS 94bE LiquidSoapAandBTanks 2017 1,585gal New ‐‐94cS 94cE LiquidSoapAandBTanks 2017 1,585gal New ‐‐94dS 94dE LiquidSoapAandBTanks 2017 1,585gal New ‐‐94eS 94eE LiquidSoapAandBTanks 2017 1,585gal New ‐‐95S 95E LiquidSoapAandBTanks 2017 1,585gal New ‐‐96S 96E LiquidSoapAandBTanks 2017 1,585gal New ‐‐97S 97E LiquidSoapAandBTanks 2017 1,585gal New ‐‐98S 98E LiquidSoapAandBTanks 2017 1,585gal New ‐‐99S 99E LiquidSoapAandBTanks 2017 1,585gal New ‐‐100S 100E LiquidSoapAandBTanks 2017 1,585gal New ‐‐101S 101E LiquidSoapAandBTanks 2017 1,585gal New ‐‐102S 102E LiquidSoapAandBTanks 2017 1,585gal New ‐‐103S 103E LiquidSoapAandBTanks 2017 1,585gal New ‐‐104S 104E LiquidSoapAandBTanks 2017 1,585gal New ‐‐105S 105E LiquidSoapAandBTanks 2017 1,585gal New ‐‐106S 106E LiquidSoapAandBTanks 2017 1,585gal New ‐‐
AttachmentIEmissionUnitsTable
(includesallemissionunitsandairpollutioncontroldevicesthatwillbepartofthispermitapplicationreview,regardlessofpermittingstatus)
Page 1 of 4Trinity Consultants
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Attachment ITabler Station
EmissionUnitID1
EmissionPointID2
EmissionUnitDescriptionYear
Installed/Modified
DesignCapacityType3anddateofChange
ControlDevice4
AttachmentIEmissionUnitsTable
(includesallemissionunitsandairpollutioncontroldevicesthatwillbepartofthispermitapplicationreview,regardlessofpermittingstatus)
107S 107E LiquidSoapAandBTanks 2017 1,585gal New ‐‐108S 108E LiquidSoapAandBTanks 2017 1,585gal New ‐‐109S 109E LiquidSoapAandBTanks 2017 1,585gal New ‐‐110S 110E LiquidSoapAandBTanks 2017 1,585gal New ‐‐111S 111E LiquidSoapAandBTanks 2017 1,585gal New ‐‐112S 112E LiquidSoapAandBTanks 2017 1,585gal New ‐‐113S 113E LiquidSoapAandBTanks 2017 1,585gal New ‐‐114S 114E LiquidSoapAandBTanks 2017 1,585gal New ‐‐115S 115E LiquidSoapAandBTanks 2017 1,585gal New ‐‐116S 116E LiquidSoapAandBTanks 2017 1,585gal New ‐‐117S 117E LiquidSoapAandBTanks 2017 1,585gal New ‐‐118S 118E LiquidSoapAandBTanks 2017 1,585gal New ‐‐119S 119E LiquidSoapAandBPacking/Filling 2017 139,798,617gal/yr New ‐‐120S Mixer1forPremixProcess1 2017 New121S Mixer2forPremixProcess1 2017 New122S PremixTank1forPremixProcess1 2017 New123S PremixTank2forPremixProcess1 2017 New124S Mixer1forLiquidSoapBProcess1 2017 New125S ProcessTank1forLiquidSoapBProcess1 2017 New126S ProcessTank2forLiquidSoapBProcess1 2017 New127S ProcessTank3forLiquidSoapBProcess1 2017 New128S Mixer1forLiquidSoapBProcess2 2017 New129S ProcessTank1forLiquidSoapBProcess2 2017 New130S ProcessTank2forLiquidSoapBProcess2 2017 New131S ProcessTank3forLiquidSoapBProcess2 2017 New132S Mixer1forLiquidSoapBProcess3 2017 New133S ProcessTank1forLiquidSoapBProcess3 2017 New134S ProcessTank2forLiquidSoapBProcess3 2017 New135S ProcessTank3forLiquidSoapBProcess3 2017 New136S PreweighStation1 2017 New137S PreweighStation2 2017 New138S PreweighStation3 2017 New139S PreweighStation4 2017 New140S PreweighStation5 2017 New141S PreweighStation6 2017 New142S PreweighStation7 2017 New143S PreweighStation8 2017 New144S SamplingStation 2017 New145S 126E HotMixTankforLiquidSoapAProcess1 2017 20,611,765cf/year New 14C146S Mixer1forLiquidSoapAProcess1 2017 New147S ProcessTank1forLiquidSoapAProcess1 2017 New148S ProcessTank2forLiquidSoapAProcess1 2017 New149S 126E HotMixTankforLiquidSoapAProcess2 2017 20,611,765cf/year New 14C150S Mixer1forLiquidSoapAProcess2 2017 New151S ProcessTank1forLiquidSoapAProcess2 2017 New152S ProcessTank2forLiquidSoapAProcess2 2017 New153S 126E HotMixTankforLiquidSoapAProcess3 2017 20,611,765cf/year New 14C154S Mixer1forLiquidSoapAProcess3 2017 New155S ProcessTank1forLiquidSoapAProcess3 2017 New156S ProcessTank2forLiquidSoapAProcess3 2017 New157S 126E HotMixTankforLiquidSoapAProcess4 2017 20,611,765cf/year New 14C158S Mixer1forLiquidSoapAProcess4 2017 New159S ProcessTank1forLiquidSoapAProcess4 2017 New160S ProcessTank2forLiquidSoapAProcess4 2017 New161S ProcessTank1forLiquidSoapBProcess4 2017 New162S ProcessTank2forLiquidSoapBProcess4 2017 New163S 132E DryConsumerLaundryandCleaningProductsATanks 2017 42,879gal New ‐‐164S 133E DryConsumerLaundryandCleaningProductsATanks 2017 37,641gal New ‐‐165S 134E DryConsumerLaundryandCleaningProductsATanks 2017 6,809gal New ‐‐166S 135E DryConsumerLaundryandCleaningProductsATanks 2017 396gal New ‐‐167S 136E DryConsumerLaundryandCleaningProductsATanks 2017 396gal New ‐‐168S 137E DryConsumerLaundryandCleaningProductsATanks 2017 396gal New ‐‐169S 138E DryConsumerLaundryandCleaningProductsATanks 2017 181gal New ‐‐170S 139E DryConsumerLaundryandCleaningProductsATanks 2017 181gal New ‐‐171S 140E DryConsumerLaundryandCleaningProductsATanks 2017 181gal New ‐‐172S 141E DryConsumerLaundryandCleaningProductsATanks 2017 181gal New ‐‐173S 142E DryConsumerLaundryandCleaningProductsATanks 2017 181gal New ‐‐174S 143E DryConsumerLaundryandCleaningProductsATanks 2017 181gal New ‐‐175S 144E DryConsumerLaundryandCleaningProductsATanks 2017 181gal New ‐‐176S 145E DryConsumerLaundryandCleaningProductsATanks 2017 181gal New ‐‐177S 146E DryConsumerLaundryandCleaningProductsATanks 2017 181gal New ‐‐178S 147E DryConsumerLaundryandCleaningProductsATanks 2017 181gal New ‐‐179S 148E DryConsumerLaundryandCleaningProductsATanks 2017 181gal New ‐‐180S 149E DryConsumerLaundryandCleaningProductsATanks 2017 181gal New ‐‐181S 150E DryConsumerLaundryandCleaningProductsATanks 2017 181gal New ‐‐182S 151E DryConsumerLaundryandCleaningProductsATanks 2017 181gal New ‐‐183S 152E DryConsumerLaundryandCleaningProductsATanks 2017 181gal New ‐‐184S 153E DryConsumerLaundryandCleaningProductsATanks 2017 181gal New ‐‐185S 154E DryConsumerLaundryandCleaningProductsATanks 2017 181gal New ‐‐186S 155E DryConsumerLaundryandCleaningProductsATanks 2017 181gal New ‐‐187S 156E DryConsumerLaundryandCleaningProductsATanks 2017 181gal New ‐‐188S 157E DryConsumerLaundryandCleaningProductsATanks 2017 181gal New ‐‐189S 158E DryConsumerLaundryandCleaningProductsAParticulateControl1 2017 17,450scfm New 15C190S 159E DryConsumerLaundryandCleaningProductsAParticulateControl2 2017 17,450scfm New 16C191S 160E DryConsumerLaundryandCleaningProductsAParticulateControl3 2017 17,450scfm New 17C192S 161E DryConsumerLaundryandCleaningProductsAParticulateControl4 2017 17,450scfm New 18C193S 162E DryConsumerLaundryandCleaningProductsAParticulateControl5 2017 17,450scfm New 19C194S 163E DryConsumerLaundryandCleaningProductsAParticulateControl6 2017 8,000scfm New 20C195S 164E DryConsumerLaundryandCleaningProductsAAdditive1 2017 109ft/s New ‐‐196S 165E Boiler1 2017 62MMBtu/hr New ‐‐197S 166E Boiler2 2017 62MMBtu/hr New ‐‐198S 167E Boiler3 2017 31MMBtu/hr New ‐‐199S 168E TemporaryBoiler 2017 11MMBtu/hr New ‐‐200S 169E CoolingTower 2017 331Mgal/hr New ‐‐201S 170E CoolingTower 2017 792Mgal/hr New ‐‐202S 171E CoolingTower 2017 212Mgal/hr New ‐‐
127E
128E
129E
130E
131E
9C
10C
11C
12C
13C
1,655,640,000scf/yr
919,800,000scf/yr
3C
121E
122E
123E
4C
5C
6C
124E
125E
525,600,000scf/yr
525,600,000scf/yr
120E
8C
7C
919,800,000scf/yr
919,800,000scf/yr
1,603,080,000scf/yr
735,840,000scf/yr
1,182,600,000scf/yr
2,496,600,000scf/yr
2,496,600,000scf/yr
Page 2 of 4Trinity Consultants
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Attachment ITabler Station
EmissionUnitID1
EmissionPointID2
EmissionUnitDescriptionYear
Installed/Modified
DesignCapacityType3anddateofChange
ControlDevice4
AttachmentIEmissionUnitsTable
(includesallemissionunitsandairpollutioncontroldevicesthatwillbepartofthispermitapplicationreview,regardlessofpermittingstatus)
203S 172E FirePumpEngine 2017 311hp New ‐‐204S 173E FirePumpEngine 2017 311hp New ‐‐205S 174E Backup/StandbyPowerGenerator 2017 350kW New ‐‐206S 175E Backup/StandbyPowerGenerator 2017 350kW New ‐‐207S 176E Backup/StandbyPowerGenerator 2017 350kW New ‐‐208S 177E FuelTanks 2017 5,000gal New ‐‐210S 179E WarehouseHeater 2017 3.05MMBtu/hr New ‐‐211S 180E WarehouseHeater 2017 3.05MMBtu/hr New ‐‐212S 181E WarehouseHeater 2017 3.05MMBtu/hr New ‐‐213S 182E WarehouseHeater 2017 3.05MMBtu/hr New ‐‐214S 183E WarehouseHeater 2017 3.05MMBtu/hr New ‐‐215S 184E WarehouseHeater 2017 3.05MMBtu/hr New ‐‐216S 185E WaterPretreatmentChemicals 2017 174,928kg/yr New ‐‐217S 186E RailcarUnloading1 2017 New 21C218S 187E RailcarUnloading2 2017 New 22C219S 188E RailcarUnloading3 2017 New 23C220S 189E RailcarUnloading4 2017 New 24C221S 190E RailcarUnloading5 2017 New 25C222S 191E StorageSilo1 2017 New ‐‐223S 192E StorageSilo2 2017 New ‐‐224S 193E StorageSilo3 2017 New ‐‐225S 194E StorageSilo4 2017 New ‐‐226S 195E StorageSilo5 2017 New ‐‐227S 196E StorageSilo6 2017 New ‐‐228S 197E StorageSilo7 2017 New ‐‐229S 198E StorageSilo8 2017 New ‐‐230S 199E StorageSilo9 2017 New ‐‐231S 200E StorageSilo10 2017 New ‐‐232S 201E StorageSilo11 2017 New ‐‐233S 202E StorageSilo12 2017 New ‐‐234S 203E StorageSilo13 2017 New ‐‐235S 204E StorageSilo14 2017 New ‐‐236S 205E StorageSilo15 2017 New ‐‐237S 206E StorageSilo16 2017 New ‐‐238S 207E StorageSilo17 2017 New ‐‐239S 208E StorageSilo18 2017 New ‐‐240S 209E StorageSilo19 2017 New ‐‐241S 210E StorageSilo20 2017 New ‐‐242S 211E StorageSilo21 2017 New ‐‐243S 212E StorageSilo22 2017 New ‐‐244S 213E StorageSilo23 2017 New ‐‐245S 214E StorageSilo24 2017 New ‐‐246S 215E PlasticRegrind 2017 32,000tons/year New 26C247S 216E FormingVOC 2017 100,000tons/year New ‐‐248S 217E PartsWashing/ProcessCleaning 2017 6tons/year New ‐‐249S 218E SpaceHeater1 2017 5MMBtu/hr New ‐‐250S 219E SpaceHeater2 2017 5MMBtu/hr New ‐‐251S 220E SpaceHeater3 2017 2.5MMBtu/hr New ‐‐252S 221E SpaceHeater4 2017 2.5MMBtu/hr New ‐‐253S 222E SpaceHeater5 2017 1MMBtu/hr New ‐‐254S 223E SpaceHeater6 2017 1MMBtu/hr New ‐‐255S 224E CoolingTower 2017 7,000gpm New ‐‐256S 225E BackupGenerator 2017 0.2MMBtu/hr New ‐‐257S 226E PrintingInk 2017 3,430lb/year New258S 227E CasePackingGlue 2017 690,080lb/year New
100,000tons/year
100,000tons/year
4)ForControlDevicesusethefollowingnumberingsystem:1C,2C,3C,...orotherappropriatedesignation.
1)ForEmissionUnits(orSources)usethefollowingnumberingsystem:1S,2S,3S,...orotherappropriatedesignation2)ForEmissionPointsusethefollowingnumberingsystem:1E,2E,3E,...orotherappropriatedesignation.3)New,modification,removal
Page 3 of 4Trinity Consultants
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Attachment ITabler Station
EmissionUnitID1
EmissionPointID2 EmissionUnitDescription
3S‐5S 3E‐5E SurfactantTanks7S‐18S 7E‐18E SurfactantTanks19S 19E SurfactantBulkLiquidTransfer
20S‐31S 20E‐31E LiquidSoapAandBTanks33S‐37S 33E‐37E LiquidSoapAandBTanks38S‐118S 38E‐118E LiquidSoapAandBTanks119S 119E LiquidSoapAandBPacking/Filling161S 131E ProcessTank1forLiquidSoapBProcess4162S 131E ProcessTank2forLiquidSoapBProcess4
163S‐188S 163E‐188E DryConsumerLaundryandCleaningProductsATanks189S 189E DryConsumerLaundryandCleaningProductsAParticulateControl1190S 190E DryConsumerLaundryandCleaningProductsAParticulateControl2191S 191E DryConsumerLaundryandCleaningProductsAParticulateControl3208S 177E FuelTanksn/a n/a HaulRoadsn/a n/a SteamVentingSystemforSanitizationofEquipmentforLiquidSoapAandBn/a n/a PMemissionsfromformingoperations‐occurinsidebuilding,noaccesstoopenair(45CSR7)n/a n/a PMemissionsfromtransportationoperations‐occurinsidebuilding,noaccesstoopenair(45CSR7)n/a n/a PrintingInkn/a n/a CasePackingGluen/a n/a Additionaldeminimissourcesfrom45CSR13,Table45‐13b
AttachmentISourcesofMinorSignificanceEmissionUnitsTable(<0.5tpy)
Page 4 of 4Trinity Consultants
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P&G – Tabler Station | R13 Permit Trinity Consultants
ATTACHMENT J
Emission Points Data Summary Sheet
Attachment JTabler Station
IDNo. Source IDNo. DeviceType ShortTerm2 Max(hr/yr) lb/hr ton/yr lb/hr ton/yr
NOX 1.6 2.3CO 6.6E‐01 2.4E‐02SO2 2.1 8.2E‐01VOC 1.8 2.1PM 2.7 1.4E+01
PM10/PM2.5 2.7 13.8H2SO4 8.5 11.7HAP 5.3E‐04 5.3E‐04NOX 1.6 2.3
CO 6.6E‐01 2.4E‐02SO2 2.1 8.2E‐01
VOC 1.8 2.0
PM 2.7 9.8PM10/PM2.5 2.7 9.8H2SO4 8.5 7.8
HAP 5.3E‐04 5.3E‐04
VOC 2.8E‐01 1.2 2.8E‐01 1.2 GasO‐EPATanks
H2SO4 3.5E‐04 1.5E‐03 3.5E‐04 1.5E‐03 GasO‐EPATanks
HAP 2.1E‐02 9.1E‐02 2.1E‐02 9.1E‐02 Gas EEVOC 1.2E‐02 5.2E‐02 1.2E‐02 5.2E‐02 Gas O‐AP‐42H2SO4 5.5E‐04 2.4E‐03 5.5E‐04 2.4E‐03 Gas O‐AP‐42
20E‐118EUpward
VerticalStackN/A
LiquidSoapAandBTanks
N/A N/A N/A N/A VOC 4.26E‐01 2.6 4.26E‐01 2.6 GasO‐EPATanks
119EUpward
VerticalStackN/A
LiquidSoapAandBPacking/Filling
N/A N/A N/A N/A VOC 2.5E‐04 1.1E‐03 2.5E‐04 1.1E‐03 Gas O‐AP‐42
PM/PM10/PM2.5 3.9E‐01 1.69 Gas EE
VOC 2.0E‐01 8.59E‐01 Gas EE
PM/PM10/PM2.5 8.1E‐01 3.6 Gas EE
VOC 3.64E‐01 1.6 Gas EE
PM/PM10/PM2.5 8.1E‐01 3.6 Gas EE
VOC 4.40E‐01 1.9 Gas EE
PM/PM10/PM2.5 5.4E‐01 2.4 Gas EE
VOC 3.64E‐01 1.6 Gas EE
PM/PM10/PM2.5 1.7E‐01 7.51E‐01 Gas EEVOC ‐‐ ‐‐ Gas EE
PM/PM10/PM2.5 1.7E‐01 7.51E‐01 Gas EEVOC ‐‐ ‐‐ Gas EE
PM/PM10/PM2.5 1.42 6.2 Gas EE
VOC 6.26 27.4 Gas MB
125EUpward
VerticalStack8C PreweighGroup2 N/A N/A N/A N/A
N/A N/A N/A Gas
AttachmentJEMISSIONPOINTSSUMMARYSHEET
Table1:EmissionsData
EmissionPointIDNo.(MustmatchEmission
UnitsTable&PlotPlan)
EmissionPointType1
EmissionUnitVentedThroughThisPoint(MustmatchEmissionUnits
Table&PlotPlan)
AirPollutionControlDevice(MustmatchEmissionUnits
Table&PlotPlan)
VentTimeforEmissionUnit(ChemicalProcessesonly)
AllRegulatedPollutants‐Chemical
Name/CAS3(SpeciateVOCsandHAPS)
MaximumPotentialUncontrolledEmissions4
MaximumPotentialControlledEmissions5
EmissionFormorPhase(At
exitconditions,Solid,LiquidorGas/Vapor)
Est.MethodUsed6
EmissionConcentration7(ppmvormg/m4)
3E‐18EUpward
VerticalStackN/A SurfactantTanks N/A N/A N/A N/A
O‐VendorandAP‐42
2EUpward
VerticalStack2C
SurfactantMakingProcess
N/A N/A N/A N/A GasO‐VendorandAP‐42
1EUpward
VerticalStack1C
SurfactantMakingProcess
N/A
120EUpward
VerticalStack3C PremixProcess1 N/A N/A N/A N/A
19EUpward
VerticalStackN/A
SurfactantBulkLiquidTransfer
N/A N/A N/A N/A
N/A N/A
122EUpward
VerticalStack5C
LiquidSoapBProcess2
N/A N/A N/A N/A
121EUpward
VerticalStack4C
LiquidSoapBProcess1
N/A N/A
N/A N/A
124EUpward
VerticalStack7C PreweighGroup1 N/A N/A N/A N/A
123EUpward
VerticalStack6C
LiquidSoapBProcess3
N/A N/A
N/A N/A127E‐130EUpward
VerticalStack9C‐12C
LiquidSoapAProcess1‐4
N/A N/A
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Attachment JTabler Station
IDNo. Source IDNo. DeviceType ShortTerm2 Max(hr/yr) lb/hr ton/yr lb/hr ton/yr
AttachmentJEMISSIONPOINTSSUMMARYSHEET
Table1:EmissionsData
EmissionPointIDNo.(MustmatchEmission
UnitsTable&PlotPlan)
EmissionPointType1
EmissionUnitVentedThroughThisPoint(MustmatchEmissionUnits
Table&PlotPlan)
AirPollutionControlDevice(MustmatchEmissionUnits
Table&PlotPlan)
VentTimeforEmissionUnit(ChemicalProcessesonly)
AllRegulatedPollutants‐Chemical
Name/CAS3(SpeciateVOCsandHAPS)
MaximumPotentialUncontrolledEmissions4
MaximumPotentialControlledEmissions5
EmissionFormorPhase(At
exitconditions,Solid,LiquidorGas/Vapor)
Est.MethodUsed6
EmissionConcentration7(ppmvormg/m4)
PM/PM10/PM2.5 2.4E‐01 1.05 Gas EE
VOC 9.9E‐03 4.3E‐02 Gas EE
PM10/PM2.5 1.5E‐02 6.5E‐02 Gas O‐AP‐42SO2 1.4E‐03 6.2E‐03 Gas O‐AP‐42NOX 2.4E‐01 1.1 Gas O‐VendorVOC 1.24 5.4 Gas MBCO 1.33 5.8 Gas O‐VendorLead 1.2E‐06 5.2E‐06 Gas O‐AP‐42
132E‐157EUpward
VerticalStackN/A
DryConsumerLaundryand
CleaningProductsATanks
N/A N/A N/A N/A VOC 1.51E‐01 6.63E‐01 1.5E‐01 6.6E‐01 Gas EE
158EUpward
VerticalStack15C
DryConsumerLaundryand
CleaningProductsAParticulateControl1
N/A N/A N/A N/A PM/PM10/PM2.5 6.9E‐02 3.0E‐01 Gas EE
159EUpward
VerticalStack16C
DryConsumerLaundryand
CleaningProductsAParticulateControl2
N/A N/A N/A N/A PM/PM10/PM2.5 4.7E‐02 2.1E‐01 Gas EE
160EUpward
VerticalStack17C
DryConsumerLaundryand
CleaningProductsAParticulateControl3
N/A N/A N/A N/A PM/PM10/PM2.6 4.5E‐02 2.0E‐01 Gas EE
161EUpward
VerticalStack18C
DryConsumerLaundryand
CleaningProductsAParticulateControl4
N/A N/A N/A N/A PM/PM10/PM2.7 1.54E+00 6.8 Gas EE
162EUpward
VerticalStack19C
DryConsumerLaundryand
CleaningProductsAParticulateControl5
N/A N/A N/A N/A PM/PM10/PM2.5 1.54E+00 6.8 Gas EE
163EUpward
VerticalStack20C
DryConsumerLaundryand
CleaningProductsAParticulateControl6
N/A N/A N/A N/A PM/PM10/PM2.5 5.57E‐01 2.4 Gas EE
164EUpward
VerticalStackN/A
DryConsumerLaundryand
CleaningProductsAAdditive1
N/A N/A N/A N/A VOC 3.6E‐01 1.6 2.0 8.7 Gas EE
N/A N/A
126EUpward
VerticalStack14C
HotMixTanksforLiquidSoapA,Process1‐4
N/A N/A N/A N/A
131EUpward
VerticalStack13C
LiquidSoapBProcess4
N/A N/A
Page 2 of 5Trinity Consultants
141801.0078
Attachment JTabler Station
IDNo. Source IDNo. DeviceType ShortTerm2 Max(hr/yr) lb/hr ton/yr lb/hr ton/yr
AttachmentJEMISSIONPOINTSSUMMARYSHEET
Table1:EmissionsData
EmissionPointIDNo.(MustmatchEmission
UnitsTable&PlotPlan)
EmissionPointType1
EmissionUnitVentedThroughThisPoint(MustmatchEmissionUnits
Table&PlotPlan)
AirPollutionControlDevice(MustmatchEmissionUnits
Table&PlotPlan)
VentTimeforEmissionUnit(ChemicalProcessesonly)
AllRegulatedPollutants‐Chemical
Name/CAS3(SpeciateVOCsandHAPS)
MaximumPotentialUncontrolledEmissions4
MaximumPotentialControlledEmissions5
EmissionFormorPhase(At
exitconditions,Solid,LiquidorGas/Vapor)
Est.MethodUsed6
EmissionConcentration7(ppmvormg/m4)
NOX 4.5 19.8 4.5 19.8
CO 2.3 10.0 2.3 10.0SO2 3.7E‐02 0.2 3.7E‐02 1.6E‐01VOC 2.2E‐01 1.0 2.2E‐01 9.8E‐01PM 2.4E‐01 1.0 2.4E‐01 1.03PM10 4.7E‐01 2.0 4.7E‐01 2.04PM2.5 4.7E‐01 2.0 4.7E‐01 2.04H2SO4 4.0E‐04 0.0 4.0E‐04 1.8E‐03HAP 1.1E‐01 0.5 1.1E‐01 5.0E‐01NOX 4.5 19.8 4.5 19.8CO 2.3 10.0 2.3 10.0SO2 3.7E‐02 1.6E‐01 3.7E‐02 1.6E‐01VOC 2.2E‐01 1.0 2.2E‐01 1.0PM 2.4E‐01 1.0 2.4E‐01 1.0PM10 4.7E‐01 2.0 4.7E‐01 2.0PM2.5 4.7E‐01 2.0 4.7E‐01 2.0H2SO4 4.0E‐04 1.8E‐03 4.0E‐04 1.8E‐03HAP 1.1E‐01 5.0E‐01 1.1E‐01 5.0E‐01
NOX 2.3 9.9 2.3 9.9
CO 1.1 5.0 1.1 5.0SO2 1.9E‐02 8.1E‐02 1.9E‐02 8.1E‐02VOC 1.1E‐01 4.9E‐01 1.1E‐01 4.9E‐01PM 1.2E‐01 0.5 1.2E‐01 0.5PM10 2.3E‐01 1.0 2.3E‐01 1.0PM2.5 2.3E‐01 1.0 2.3E‐01 1.0H2SO4 2.0E‐04 8.8E‐04 2.0E‐04 8.8E‐04HAP 5.7E‐02 2.5E‐01 5.7E‐02 2.5E‐01
168EUpward
VerticalStackN/A TemporaryBoiler N/A N/A N/A N/A N/A N/A N/A N/A N/A Gas N/A
169E‐171EUpward
VerticalStackN/A CoolingTower N/A N/A N/A N/A PM/PM10/PM2.5 8.91E‐01 3.9 8.91E‐01 3.9 Gas O‐AP‐42
NOX 3.6 8.9E‐01 3.6 8.9E‐01
CO 1.1 2.7E‐01 1.1 2.7E‐01SO2 1.9E‐03 4.8E‐04 1.9E‐03 4.8E‐04VOC 1.4E‐01 3.4E‐02 1.4E‐01 3.4E‐02PM 1.4E‐01 3.4E‐02 1.4E‐01 3.4E‐02PM10 1.4E‐01 3.4E‐02 1.4E‐01 3.4E‐02PM2.5 1.4E‐01 3.4E‐02 1.4E‐01 3.4E‐02HAP 2.8E‐02 7.0E‐03 2.8E‐02 7.0E‐03
NOX 10.5 2.6 10.5 2.6
CO 1.7 4.2E‐01 1.7 4.2E‐01SO2 4.4E‐03 1.1E‐03 4.37E‐03 1.1E‐03VOC 1.3E‐01 3.3E‐02 1.31E‐01 3.3E‐02PM 1.4E‐01 3.6E‐02 1.44E‐01 3.6E‐02PM10 1.4E‐01 3.5E‐02 1.38E‐01 3.5E‐02PM2.5 1.4E‐01 3.5E‐02 1.38E‐01 3.5E‐02HAP 6.4E‐02 1.6E‐02 6.38E‐02 1.6E‐02
177EUpward
VerticalStackN/A FuelTanks N/A N/A N/A N/A VOC 5.2E‐04 2.3E‐03 5.2E‐04 2.3E‐03 Gas
O‐EPATanks
O‐AP‐42166EUpward
VerticalStackN/A Boiler2 N/A Gas
O‐Vendor
O‐AP‐42
Gas O‐AP‐42
Gas O‐Vendor
Gas
Gas
172E‐173EUpward
VerticalStackN/A FirePumpEngine N/A N/A N/A N/A
174E‐176EUpward
VerticalStackN/A
Backup/StandbyPowerGenerator
N/A N/A N/A N/A
N/A Boiler3 N/A N/A N/A N/A
N/A N/A N/A
UpwardVerticalStack
N/A Boiler1 N/A N/A N/A N/A
167EUpward
VerticalStack
165E
Page 3 of 5Trinity Consultants
141801.0078
Attachment JTabler Station
IDNo. Source IDNo. DeviceType ShortTerm2 Max(hr/yr) lb/hr ton/yr lb/hr ton/yr
AttachmentJEMISSIONPOINTSSUMMARYSHEET
Table1:EmissionsData
EmissionPointIDNo.(MustmatchEmission
UnitsTable&PlotPlan)
EmissionPointType1
EmissionUnitVentedThroughThisPoint(MustmatchEmissionUnits
Table&PlotPlan)
AirPollutionControlDevice(MustmatchEmissionUnits
Table&PlotPlan)
VentTimeforEmissionUnit(ChemicalProcessesonly)
AllRegulatedPollutants‐Chemical
Name/CAS3(SpeciateVOCsandHAPS)
MaximumPotentialUncontrolledEmissions4
MaximumPotentialControlledEmissions5
EmissionFormorPhase(At
exitconditions,Solid,LiquidorGas/Vapor)
Est.MethodUsed6
EmissionConcentration7(ppmvormg/m4)
NOX 9.0E‐01 3.93 9.0E‐01 3.9
CO 1.51 6.60 1.51 6.60SO2 1.1E‐02 4.7E‐02 1.1E‐02 4.7E‐02VOC 9.9E‐02 4.3E‐01 9.9E‐02 4.3E‐01PM 1.4E‐01 6.0E‐01 1.4E‐01 6.0E‐01PM10 1.4E‐01 6.0E‐01 1.4E‐01 6.0E‐01PM2.5 1.4E‐01 6.0E‐01 1.4E‐01 6.0E‐01H2SO4 1.2E‐04 5.1E‐04 1.2E‐04 5.1E‐04HAP 3.4E‐02 1.5E‐01 3.4E‐02 1.5E‐01VOC 3.0 13.0 3.0 13.0HAP 9.1E‐04 4.0E‐03 9.1E‐04 4.0E‐03PM 7.99E‐01 3.50 7.99E‐02 3.50E‐01PM10 7.99E‐01 3.50 7.99E‐02 3.50E‐01PM2.5 7.99E‐01 3.50 7.99E‐02 3.50E‐01PM 7.99E‐01 3.50 7.99E‐01 3.5PM10 7.99E‐01 3.50 7.99E‐01 3.5PM2.5 7.99E‐01 3.50 7.99E‐01 3.5PM 7.67E‐01 3.36 3.84E‐02 1.68E‐01PM10 7.67E‐01 3.36 3.84E‐02 1.68E‐01PM2.5 7.67E‐01 3.36 3.84E‐02 1.68E‐01
216EUpward
VerticalStackN/A FormingVOC N/A N/A N/A N/A VOC 7.01E‐01 3.07 7.01E‐01 3.1 Gas O‐Vendor
217EUpward
VerticalStackN/A
PartsWashing/Process
CleaningN/A N/A N/A N/A VOC 1.4E+00 6.00 1.4 6.0 Gas O‐Vendor
NOX 8.33E‐01 3.7 8.33E‐01 3.7CO 1.4 6.1 1.4 6.1SO2 1.0E‐02 4.4E‐02 1.00E‐02 4.38E‐02VOC 9.2E‐02 4.0E‐01 9.17E‐02 4.02E‐01PM 1.3E‐01 5.5E‐01 1.27E‐01 5.55E‐01PM10 1.3E‐01 5.5E‐01 1.27E‐01 5.55E‐01PM2.5 1.3E‐01 5.5E‐01 1.27E‐01 5.55E‐01H2SO4 1.1E‐04 4.7E‐04 1.08E‐04 4.75E‐04HAP 3.1E‐02 1.3E‐01 3.15E‐02 1.30E‐01PM 2.8E‐01 1.2 2.80E‐01 1.2PM10 2.8E‐01 1.2 2.80E‐01 1.2PM2.5 2.8E‐01 1.2 2.80E‐01 1.2NOX 4.17E‐01 1.04E‐01 4.17E‐01 1.04E‐01CO 8.33E‐01 2.08E‐01 8.33E‐01 2.08E‐01SO2 1.18E‐04 2.94E‐05 1.18E‐04 2.94E‐05VOC 2.01E‐01 5.02E‐02 2.01E‐01 5.02E‐02PM 1.90E‐03 4.75E‐04 1.90E‐03 4.75E‐04PM10 3.88E‐03 9.71E‐04 3.88E‐03 9.71E‐04PM2.5 3.88E‐03 9.71E‐04 3.88E‐03 9.71E‐04HAP 6.48E‐03 1.62E‐03 6.48E‐03 1.62E‐03VOC 8.65E‐02 3.79E‐01 8.7E‐02 3.79E‐01 Gas EEHAP 3.65E‐02 1.60E‐01 3.7E‐02 1.60E‐01 Gas EEVOC 4.73E‐02 2.07E‐01 4.7E‐02 2.07E‐01 Gas EEHAP 1.58E‐03 6.90E‐03 1.6E‐03 6.90E‐03 Gas EE
EE185E Fugitive N/AWaterPretreatment
ChemicalsN/A N/A N/A N/A Gas
Gas O‐AP‐42179E‐184EUpward
VerticalStackN/A WarehouseHeater N/A N/A N/A N/A
Gas
UpwardVerticalStack
21C‐25C RailcarUnloading N/A
N/A
N/A
O‐Vendor215EUpward
VerticalStackN/A PlasticRegrind N/A
186E‐190E
O‐Vendor
N/A N/A Gas O‐Vendor
191E‐214EUpward
VerticalStackN/A StorageSilo N/A
N/A
N/A N/A Gas
Gas O‐AP‐42
224EUpward
VerticalStackN/A CoolingTower N/A N/A N/A N/A
218E‐223EUpward
VerticalStackN/A SpaceHeater N/A N/A N/A
N/A N/A N/A
Gas O‐AP‐42
Gas O‐AP‐42
225EUpward
VerticalStackN/A BackupGenerator N/A N/A N/A N/A
226E Fugitive N/A PrintingInk N/A N/A N/A N/A
227E Fugitive N/A CasePackingGlue N/A N/A N/A N/A
Page 4 of 5Trinity Consultants
141801.0078
Attachment JTabler Station
Temp.(of)
VolumetricFlow1(acfm)atoperatingconditions
Velocity(fps)
GroundLevel(Height
abovemeansealevel)
StackHeight2
(Releaseheightofemissionsabovegroundlevel)
Northing Easting
1E TBD TBD TBD TBD TBD TBD 4,366 7572E TBD TBD TBD TBD TBD TBD 4,366 757
3E‐18E N/A N/A N/A N/A N/A N/A N/A N/A19E N/A N/A N/A N/A N/A N/A N/A N/A
20E‐118E N/A N/A N/A N/A N/A N/A N/A N/A119E N/A N/A N/A N/A N/A N/A N/A N/A120E TBD TBD TBD TBD TBD TBD 4,366 757121E TBD TBD TBD TBD TBD TBD 4,366 757122E TBD TBD TBD TBD TBD TBD 4,366 757123E TBD TBD TBD TBD TBD TBD 4,366 757124E TBD TBD TBD TBD TBD TBD 4,366 757125E TBD TBD TBD TBD TBD TBD 4,366 757
127E‐130E TBD TBD TBD TBD TBD TBD 4,366 757131E TBD TBD TBD TBD TBD TBD 4,366 757126E TBD TBD TBD TBD TBD TBD 4,366 757
132E‐157E N/A N/A N/A N/A N/A N/A N/A N/A158E TBD TBD TBD TBD TBD TBD 4,366 757159E TBD TBD TBD TBD TBD TBD 4,366 757160E TBD TBD TBD TBD TBD TBD 4,366 757161E TBD TBD TBD TBD TBD TBD 4,366 757162E TBD TBD TBD TBD TBD TBD 4,366 757163E TBD TBD TBD TBD TBD TBD 4,366 757164E N/A N/A N/A N/A N/A N/A N/A N/A165E TBD TBD TBD TBD TBD TBD 4,366 757166E TBD TBD TBD TBD TBD TBD 4,366 757167E TBD TBD TBD TBD TBD TBD 4,366 757168E TBD TBD TBD TBD TBD TBD 4,366 757
169E‐171E TBD TBD TBD TBD TBD TBD 4,366 757172E‐173E N/A N/A N/A N/A N/A N/A N/A N/A174E‐176E N/A N/A N/A N/A N/A N/A N/A N/A
177E N/A N/A N/A N/A N/A N/A N/A N/A179E‐184E N/A N/A N/A N/A N/A N/A N/A N/A
185E N/A N/A N/A N/A N/A N/A N/A N/A186E‐190E TBD TBD TBD TBD TBD TBD 4,366 757191E‐214E TBD TBD TBD TBD TBD TBD 4,366 757
215E TBD TBD TBD TBD TBD TBD 4,366 757216E N/A N/A N/A N/A N/A N/A N/A N/A217E N/A N/A N/A N/A N/A N/A N/A N/A
218E‐223E N/A N/A N/A N/A N/A N/A N/A N/A224E TBD TBD TBD TBD TBD TBD 4,366 757225E N/A N/A N/A N/A N/A N/A N/A N/A226E N/A N/A N/A N/A N/A N/A N/A N/A227E N/A N/A N/A N/A N/A N/A N/A N/A
AttachmentJ
EMISSIONPOINTSSUMMARYSHEET
Table2:ReleaseParameterData
EmissionPointIDNo.(MustmatchEmission
UnitsTable)
InnerDiameter(ft.)
ExitGas EmissionPointElevation(ft) UTMCoordinates(km)
Page 5 of 5Trinity Consultants
141801.0078
P&G – Tabler Station | R13 Permit Trinity Consultants
ATTACHMENT K
Fugitive Emissions Data Summary Sheet
Attachment KTabler Station
Question YES/NO ifYES:
1 Willtherebehaulroadactivities? Yes Completehaulroademissionsunitdatasheet
2 Willtherebestoragepiles? NoCompleteTable1ofnonmetallicmineralsprocessingemissionsunitdatasheet
3 Willtherebeliquidloading/unloadingoperations? YesCompletebulkliquidtransferoperations
emissionsunitdatasheet
4Willtherebeemissionsofairpollutantsfromwastewater
treatmentevaporation?Yes Completegeneralemissionsunitdatasheet
5
Willtherebeequipmentleaks(e.g.leaksfrompumps,compressors,in‐lineprocessvalves,pressurereliefdevices,open‐endedvalves,samplingconnections,flanges,agitators,
coolingtowers,etc.)?
NoCompleteleaksourcedatasheetsectionofthechemicalprocessesemissionsunitdatasheet
6 WilltherebeGeneralClean‐upVOCOperations? Yes Completethegeneralemissionsunitdatasheet
7Willtherebeanyotheractivitiesthatgeneratefugitive
emissions?Yes
Completethegeneralemissionsunitdatasheetormostappropriateform
AttachmentKFUGITIVEEMISSIONSDATASUMMARYSHEET
Page 1 of 2Trinity Consultants
141801.0078
Attachment KTabler Station
lb/hr ton/yr lb/hr ton/yrHaulRoad/RoadDustEmissions NA NA NA NA NA NA
PavedHaulRoads PM 5.0E‐04 2.2E‐03 N/A N/A O‐AP‐42UnpavedHaulRoads NA NA NA NA NA NAStoragePileEmissions NA NA NA NA NA NA
VOC 1.2E‐02 5.2E‐02 1.2E‐02 5.2E‐02H2SO4 5.5E‐04 2.4E‐03 5.5E‐04 2.4E‐03
VOC 3.0 13.0 3.0 13.0EE‐
EngineeringEstimate
HAP 9.1E‐04 4.0E‐03 9.1E‐04 4.0E‐03EE‐
EngineeringEstimate
EquipmentLeaks NA NA NA NA NA NA
GeneralClean‐upVOCEmissions67‐63‐0,and
others1.37 6.00 1.37 6.00
EE‐EngineeringEstimate
VOC 8.7E‐02 3.79E‐01 8.65E‐02 3.79E‐01
GlycolEther 3.7E‐02 1.60E‐01 3.65E‐02 1.60E‐01
VOC 4.7E‐02 2.07E‐01 4.73E‐02 2.07E‐01
108‐05‐4 1.6E‐03 6.90E‐03 1.58E‐03 6.90E‐03Other NA‐FugitiveemissionsfromtanksarecalculatedinAttachmentL
WastewaterTreatmentEvaporation&Operations
Loading/UnloadingOperations O‐AP‐42
AttachmentKFUGITIVEEMISSIONSDATASUMMARYSHEET
FUGITIVEEMISSIONSSUMMARY
AllRegulatedPollutants‐
ChemicalName/CAS
MaximumPotentialUncontrolledEmissions
MaximumPotentialControlledEmissions Est.Method
Used
InkPrinters
CasePackingGlue
EE‐EngineeringEstimate
EE‐EngineeringEstimate
Page 2 of 2Trinity Consultants
141801.0078
P&G – Tabler Station | R13 Permit Trinity Consultants
ATTACHMENT L
Emission Unit Data Sheet
Attachment LTabler Station
1 3 4 6 8 9A 9B 10A 13A 18 20 22A 22B 22C 27 38B 39C 39D 40
BulkStorageAreaName
TankEquipmentIdentificationNumber
EmissionPointIdentificationNumber
TypeofChange
Capacity(gallons)
InternalDiameter
(ft)
InternalHeight(ft)
MaxLiquidHeight
MaxAnnualThroughput(gal/yr)
TypeofTankShell
Color/RoofColor
AretheTanksHeated?
Providetheoperating
temperature(F)
Describehowheatisprovidedtothetank
City/StateforTANKS
calculations
MaxVaporPressure(psi)
LiquidDensity(lb/gal)
LiquidMolecularWeight
(lb/lb‐mol)
EmissionControlDevices
MaterialClassification
AnnualLoss
(lb/year)
MaterialClassificati
on
AnnualLoss
(lb/year)
EstimationMethod
SurfactantTanks 3S 3E NewConst. 120,762 21.3 45.5 41.6 20,327,735VerticalFixed
RoofAboveground
Grey/Grey Yes 90.5SteamorHotWater
DullesAirport,
WashingtonDC
3.50E‐03 6.84 197Doesnotapply
VOC 109.6 HAP n/a EPA
SurfactantTanks 4S 4E NewConst. 48,345 13.5 45.5 41.6 8,805,475VerticalFixed
RoofAboveground
Grey/Grey Yes 89.6SteamorHotWater
DullesAirport,
WashingtonDC
3.42E‐03 7.18 197Doesnotapply
VOC 44.6 HAP 44.6 EPA
SurfactantTanks 5S 5E NewConst. 40,109 13.5 37.7 37.3 9,481,192VerticalFixed
RoofAboveground
Grey/Grey Yes 95SteamorHotWater
DullesAirport,
WashingtonDC
3.92E‐03 7.68 197Doesnotapply
VOC 48.3 HAP 48.3 EPA
SurfactantTanks 6S 6E NewConst. 40,109 13.5 37.7 37.3 1,917,922VerticalFixed
RoofAboveground
Grey/Grey Yes Ambient N/A
DullesAirport,
WashingtonDC
8.62E‐01 6.58 46.07Doesnotapply
VOC 1722.7 HAP n/a EPA
SurfactantTanks 7S 7E NewConst. 15,125 9.8 26.6 26.5 7,823,046VerticalFixed
RoofAboveground
Grey/Grey Yes 99.5SteamorHotWater
DullesAirport,
WashingtonDC
1.50E‐03 8.69 323Doesnotapply
VOC 19.0 HAP 4.0 EPA
SurfactantTanks 8S 8E NewConst. 15,125 9.8 26.6 26.5 7,823,046VerticalFixed
RoofAboveground
Grey/Grey Yes 95SteamorHotWater
DullesAirport,
WashingtonDC
1.50E‐03 8.69 323Doesnotapply
VOC 19.1 HAP 4.0 EPA
SurfactantTanks 9S 9E NewConst. 15,125 9.8 26.6 26.5 6,841,173VerticalFixed
RoofAboveground
Grey/Grey Yes 95SteamorHotWater
DullesAirport,
WashingtonDC
1.50E‐03 8.69 323Doesnotapply
VOC 17.3 HAP n/a EPA
SurfactantTanks 10S 10E NewConst. 72,475 16.5 45.5 41.6 39,115,231VerticalFixed
RoofAboveground
Grey/Grey Yes 99.5SteamorHotWater
DullesAirport,
WashingtonDC
1.32E‐03 8.35 323Doesnotapply
VOC 82.6 HAP 20.2 EPA
SurfactantTanks 11S 11E NewConst. 72,475 16.5 45.5 41.6 39,115,231VerticalFixed
RoofAboveground
Grey/Grey Yes 99.5SteamorHotWater
DullesAirport,
WashingtonDC
1.32E‐03 8.35 323Doesnotapply
VOC 82.6 HAP 20.2 EPA
SurfactantTanks 12S 12E NewConst. 72,475 16.5 45.5 41.6 39,115,231VerticalFixed
RoofAboveground
Grey/Grey Yes 95SteamorHotWater
DullesAirport,
WashingtonDC
1.24E‐03 8.35 323Doesnotapply
VOC 78.5 HAP 20.2 EPA
SurfactantTanks 13S 13E NewConst. 72,475 16.5 45.5 41.6 39,115,231VerticalFixed
RoofAboveground
Grey/Grey Yes 95SteamorHotWater
DullesAirport,
WashingtonDC
1.24E‐03 8.35 323Doesnotapply
VOC 78.5 HAP 20.2 EPA
SurfactantTanks 14S 14E NewConst. 72,475 16.5 45.5 41.6 34,205,863VerticalFixed
RoofAboveground
Grey/Grey Yes 95SteamorHotWater
DullesAirport,
WashingtonDC
1.24E‐03 8.35 323Doesnotapply
VOC 71.1 HAP n/a EPA
SurfactantTanks 15S 15E NewConst. 72,475 16.5 45.5 41.6 34,205,863VerticalFixed
RoofAboveground
Grey/Grey Yes 95SteamorHotWater
DullesAirport,
WashingtonDC
1.24E‐03 8.35 323Doesnotapply
VOC 71.1 HAP n/a EPA
SurfactantTanks 16S 16E NewConst. 26,083 11.8 31.8 30.6 115,491VerticalFixed
RoofAboveground
Grey/Grey Yes 95SteamorHotWater
DullesAirport,
WashingtonDC
1.50E‐03 8.69 323Doesnotapply
VOC 1.3 HAP n/a EPA
SurfactantTanks 17S 17E NewConst. 15,125 9.8 26.6 26.5 2,000,000VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHotWater
DullesAirport,
WashingtonDC
1.69E‐03 15.36 98.09Doesnotapply
H2SO4 3.0 HAP n/a EPA
SurfactantTanks 18S 18E NewConst. 15,125 9.8 26.6 26.5 150,000VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHotWater
DullesAirport,
WashingtonDC
1.69E‐03 15.36 98.09Doesnotapply
VOC 0.6 HAP n/a EPA
LiquidSoapAandBTanks
20S 20E NewConst. 39,626 13.5 36.1 23.8 13,431,682VerticalFixed
RoofAboveground
Grey/Grey Yes 113SteamorHotWater
DullesAirport,
WashingtonDC
1.32E‐03 8.35 323Doesnotapply
VOC 31.5 HAP 6.9 EPA
41
AttachmentLEMISSIONSUNITDATASHEET‐STORAGETANKS
Page 1 of 16Trinity Consultants
141801.0078
Attachment LTabler Station
1 3 4 6 8 9A 9B 10A 13A 18 20 22A 22B 22C 27 38B 39C 39D 40
BulkStorageAreaName
TankEquipmentIdentificationNumber
EmissionPointIdentificationNumber
TypeofChange
Capacity(gallons)
InternalDiameter
(ft)
InternalHeight(ft)
MaxLiquidHeight
MaxAnnualThroughput(gal/yr)
TypeofTankShell
Color/RoofColor
AretheTanksHeated?
Providetheoperating
temperature(F)
Describehowheatisprovidedtothetank
City/StateforTANKS
calculations
MaxVaporPressure(psi)
LiquidDensity(lb/gal)
LiquidMolecularWeight
(lb/lb‐mol)
EmissionControlDevices
MaterialClassification
AnnualLoss
(lb/year)
MaterialClassificati
on
AnnualLoss
(lb/year)
EstimationMethod
41
AttachmentLEMISSIONSUNITDATASHEET‐STORAGETANKS
LiquidSoapAandBTanks
21S 21E NewConst. 39,626 13.5 36.1 23.8 24,833,180VerticalFixed
RoofAboveground
Grey/Grey Yes 113SteamorHotWater
DullesAirport,
WashingtonDC
1.24E‐03 8.35 323Doesnotapply
VOC 46.3 HAP 12.8 EPA
LiquidSoapAandBTanks
22S 22E NewConst. 39,626 13.5 36.1 23.8 18,189,304VerticalFixed
RoofAboveground
Grey/Grey Yes 113SteamorHotWater
DullesAirport,
WashingtonDC
1.24E‐03 8.35 323Doesnotapply
VOC 36.6 HAP n/a EPA
LiquidSoapAandBTanks
23S 23E NewConst. 7,925 7.9 21.0 13.9 291,058VerticalFixed
RoofAboveground
Grey/Grey Yes 113SteamorHotWater
DullesAirport,
WashingtonDC
1.24E‐03 8.35 323Doesnotapply
VOC 2.4 HAP 2.4 EPA
LiquidSoapAandBTanks
24S 24E NewConst. 7,925 7.9 21.0 13.9 229,500VerticalFixed
RoofAboveground
Grey/Grey Yes 113SteamorHotWater
DullesAirport,
WashingtonDC
2.03E‐01 9.16 36Doesnotapply
VOC n/a HAP 37.0 EPA
LiquidSoapAandBTanks
25S 25E NewConst. 39,626 13.5 36.1 23.8 46,050,900VerticalFixed
RoofAboveground
Grey/Grey Yes 113SteamorHotWater
DullesAirport,
WashingtonDC
9.28E‐17 0.88 343Doesnotapply
VOC 6.10E‐12 HAP n/a EPA
LiquidSoapAandBTanks
26S 26E NewConst. 15,850 9.8 26.6 17.5 685,694VerticalFixed
RoofAboveground
Grey/Grey Yes 113SteamorHotWater
DullesAirport,
WashingtonDC
n/a 7.51 503Doesnotapply
VOC 0.00E+00 HAP n/a EPA
LiquidSoapAandBTanks
27S 27E NewConst. 39,626 13.5 36.1 23.8 2,317,226VerticalFixed
RoofAboveground
Grey/Grey Yes 113SteamorHotWater
DullesAirport,
WashingtonDC
1.60E‐03 8.97 388Doesnotapply
VOC 20.7 HAP n/a EPA
LiquidSoapAandBTanks
28S 28E NewConst. 26,417 11.8 31.8 21.0 2,012,364VerticalFixed
RoofAboveground
Grey/Grey Yes 113SteamorHotWater
DullesAirport,
WashingtonDC
1.93E‐04 6.78 270Doesnotapply
VOC 1.3 HAP n/a EPA
LiquidSoapAandBTanks
29S 29E NewConst. 15,850 9.8 26.6 17.5 1,039,693VerticalFixed
RoofAboveground
Grey/Grey Yes 113SteamorHotWater
DullesAirport,
WashingtonDC
1.16E‐07 6.77 242Doesnotapply
VOC 3.84E‐04 HAP n/a EPA
LiquidSoapAandBTanks
30S 30E NewConst. 26,417 11.8 31.8 21.0 1,646,085VerticalFixed
RoofAboveground
Grey/Grey Yes 113SteamorHotWater
DullesAirport,
WashingtonDC
7.25E‐05 8.35 503Doesnotapply
VOC 8.39E‐01 HAP n/a EPA
LiquidSoapAandBTanks
31S 31E NewConst. 15,850 9.8 26.6 17.5 1,691,510VerticalFixed
RoofAboveground
Grey/Grey Yes 113SteamorHotWater
DullesAirport,
WashingtonDC
3.30E‐02 8.35 503Doesnotapply
VOC 265.6 HAP n/a EPA
LiquidSoapAandBTanks
32S 32E NewConst. 15,850 9.8 26.6 17.5 240,216VerticalFixed
RoofAboveground
Grey/Grey Yes 113SteamorHotWater
DullesAirport,
WashingtonDC
8.13E‐01 7.93 368Doesnotapply
VOC 1563.9 HAP n/a EPA
LiquidSoapAandBTanks
33S 33E NewConst. 7,925 7.9 21.0 13.9 282,057VerticalFixed
RoofAboveground
Grey/Grey No 77SteamorHotWater
DullesAirport,
WashingtonDC
4.83E‐05 10.52 92Doesnotapply
VOC 2.85E‐02 HAP n/a EPA
LiquidSoapAandBTanks
34S 34E NewConst. 7,925 9.0 23.4 15.4 146,204VerticalFixed
RoofAboveground
Grey/Grey No Ambient N/A
DullesAirport,
WashingtonDC
5.00E‐01 8.71 200Doesnotapply
VOC 634.5 HAP 3.2 EPA
LiquidSoapAandBTanks
35S 35E NewConst. 7,925 9.0 23.4 15.4 47,372VerticalFixed
RoofAboveground
Grey/Grey No Ambient N/A
DullesAirport,
WashingtonDC
5.00E‐01 8.71 200Doesnotapply
VOC 394.5 HAP 2.0 EPA
LiquidSoapAandBTanks
36S 36E NewConst. 7,925 9.0 23.4 15.4 38,244VerticalFixed
RoofAboveground
Grey/Grey No Ambient N/A
DullesAirport,
WashingtonDC
5.00E‐01 8.71 200Doesnotapply
VOC 372.4 HAP 1.9 EPA
LiquidSoapAandBTanks
37S 37E NewConst. 7,925 9.0 23.4 15.4 7,552VerticalFixed
RoofAboveground
Grey/Grey Yes Ambient N/A
DullesAirport,
WashingtonDC
5.00E‐01 8.71 200Doesnotapply
VOC 297.8 HAP 1.5 EPA
Page 2 of 16Trinity Consultants
141801.0078
Attachment LTabler Station
1 3 4 6 8 9A 9B 10A 13A 18 20 22A 22B 22C 27 38B 39C 39D 40
BulkStorageAreaName
TankEquipmentIdentificationNumber
EmissionPointIdentificationNumber
TypeofChange
Capacity(gallons)
InternalDiameter
(ft)
InternalHeight(ft)
MaxLiquidHeight
MaxAnnualThroughput(gal/yr)
TypeofTankShell
Color/RoofColor
AretheTanksHeated?
Providetheoperating
temperature(F)
Describehowheatisprovidedtothetank
City/StateforTANKS
calculations
MaxVaporPressure(psi)
LiquidDensity(lb/gal)
LiquidMolecularWeight
(lb/lb‐mol)
EmissionControlDevices
MaterialClassification
AnnualLoss
(lb/year)
MaterialClassificati
on
AnnualLoss
(lb/year)
EstimationMethod
41
AttachmentLEMISSIONSUNITDATASHEET‐STORAGETANKS
LiquidSoapAandBTanks
50S 50E NewConst. 7,925 9.0 23.4 15.4 696,309VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
1.24E‐03 8.35 323Doesnotapply
VOC 4.2 HAP n/a EPA
LiquidSoapAandBTanks
56S 56E NewConst. 7,275 9.0 23.4 15.4 287,453VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
1.59E‐03 9.09 76Doesnotapply
VOC 8.04E‐01 HAP n/a EPA
LiquidSoapAandBTanks
53S 53E NewConst. 7,925 9.0 23.4 15.4 112,722VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
1.24E‐03 8.35 323Doesnotapply
VOC 1.05E+00 HAP n/a EPA
LiquidSoapAandBTanks
38S 38E NewConst. 396 3.3 8.58 5.6628 37,808VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
8.13E‐01 8.50 503Doesnotapply
VOC 216.2 HAP n/a EPA
LiquidSoapAandBTanks
40S 40E NewConst. 396 3.3 8.58 5.6628 16,874VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
5.61E‐02 12.02 292Doesnotapply
VOC 6.4 HAP n/a EPA
LiquidSoapAandBTanks
41S 41E NewConst. 396 3.3 8.58 5.6628 12,883VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
2.90E‐10 10.01 205Doesnotapply
VOC 1.78E‐08 HAP n/a EPA
LiquidSoapAandBTanks
42S 42E NewConst. 396 3.3 8.58 5.6628 8,007VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
8.13E‐01 8.96 233Doesnotapply
VOC 35.2 HAP n/a EPA
LiquidSoapAandBTanks
43S 43E NewConst. 396 3.3 8.58 5.6628 147,994VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
8.13E‐01 7.93 503Doesnotapply
VOC 390.6 HAP n/a EPA
LiquidSoapAandBTanks
44S 44E NewConst. 396 3.3 8.58 5.6628 11,983VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
8.13E‐01 8.68 503Doesnotapply
VOC 113.8 HAP n/a EPA
LiquidSoapAandBTanks
45S 45E NewConst. 396 3.3 8.58 5.6628 121,569VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
1.82E‐03 8.71 108Doesnotapply
VOC 1.68E‐01 HAP n/a EPA
LiquidSoapAandBTanks
46S 46E NewConst. 396 3.3 8.58 5.6628 14,581VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
4.50E‐01 8.31 503Doesnotapply
VOC 76.6 HAP n/a EPA
LiquidSoapAandBTanks
47S 47E NewConst. 396 3.3 8.58 5.6628 8,418VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
8.13E‐01 8.35 503Doesnotapply
VOC 79.9 HAP n/a EPA
LiquidSoapAandBTanks
51S 51E NewConst. 396 3.3 8.58 5.6628 n/aVerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
n/a n/a n/aDoesnotapply
VOC n/a HAP n/a EPA
LiquidSoapAandBTanks
52S 52E NewConst. 396 3.3 8.58 5.6628 990VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
1.24E‐03 8.35 323Doesnotapply
VOC 9.24E‐03 HAP n/a EPA
LiquidSoapAandBTanks
54S 54E NewConst. 660 3.3 8.58 5.6628 267,217VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
1.24E‐03 8.35 323Doesnotapply
VOC 5.69E‐01 HAP n/a EPA
LiquidSoapAandBTanks
55S 55E NewConst. 396 3.3 8.58 5.6628 75VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
8.13E‐01 8.50 503Doesnotapply
VOC 7.09E‐01 HAP n/a EPA
LiquidSoapAandBTanks
57S 57E NewConst. 1,057 3.3 8.58 5.6628 24,591VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
1.59E‐03 9.09 76Doesnotapply
VOC 5.75E‐02 HAP n/a EPA
Page 3 of 16Trinity Consultants
141801.0078
Attachment LTabler Station
1 3 4 6 8 9A 9B 10A 13A 18 20 22A 22B 22C 27 38B 39C 39D 40
BulkStorageAreaName
TankEquipmentIdentificationNumber
EmissionPointIdentificationNumber
TypeofChange
Capacity(gallons)
InternalDiameter
(ft)
InternalHeight(ft)
MaxLiquidHeight
MaxAnnualThroughput(gal/yr)
TypeofTankShell
Color/RoofColor
AretheTanksHeated?
Providetheoperating
temperature(F)
Describehowheatisprovidedtothetank
City/StateforTANKS
calculations
MaxVaporPressure(psi)
LiquidDensity(lb/gal)
LiquidMolecularWeight
(lb/lb‐mol)
EmissionControlDevices
MaterialClassification
AnnualLoss
(lb/year)
MaterialClassificati
on
AnnualLoss
(lb/year)
EstimationMethod
41
AttachmentLEMISSIONSUNITDATASHEET‐STORAGETANKS
LiquidSoapAandBTanks
59S 59E NewConst. 396 3.3 8.58 5.6628 2,260VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
1.59E‐03 9.09 76Doesnotapply
VOC 6.32E‐03 HAP n/a EPA
LiquidSoapAandBTanks
60S 60E NewConst. 132 2.3 5.98 3.9468 1,953VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
5.80E‐04 8.41 138Doesnotapply
VOC 3.63E‐03 HAP 0.0 EPA
LiquidSoapAandBTanks
61S 61E NewConst. 396 3.3 8.58 5.6628 175,632VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
8.13E‐01 8.31 503Doesnotapply
VOC 434.4 HAP n/a EPA
LiquidSoapAandBTanks
63S 63E NewConst. 396 3.3 8.58 5.6628 38,430VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
3.40E‐01 7.59 503Doesnotapply
VOC 90.8 HAP n/a EPA
LiquidSoapAandBTanks
64S 64E NewConst. 396 3.3 8.58 5.6628 15,482VerticalFixed
RoofAboveground
Grey/Grey Yes 74SteamorHot
Water
DullesAirport,
WashingtonDC
1.20E‐01 8.71 200Doesnotapply
VOC 8.7 HAP 4.34E‐02 EPA
LiquidSoapAandBTanks
65S 65E NewConst. 396 3.3 8.58 5.6628 14,619VerticalFixed
RoofAboveground
Grey/Grey Yes 74SteamorHot
Water
DullesAirport,
WashingtonDC
1.20E‐01 8.71 200Doesnotapply
VOC 8.2 HAP 4.09E‐02 EPA
LiquidSoapAandBTanks
66S 66E NewConst. 396 3.3 8.58 5.6628 24,900VerticalFixed
RoofAboveground
Grey/Grey Yes 74SteamorHot
Water
DullesAirport,
WashingtonDC
1.20E‐01 8.71 200Doesnotapply
VOC 11.6 HAP 5.78E‐02 EPA
LiquidSoapAandBTanks
67S 67E NewConst. 396 3.3 8.58 5.6628 48,605VerticalFixed
RoofAboveground
Grey/Grey Yes 74SteamorHot
Water
DullesAirport,
WashingtonDC
1.20E‐01 8.71 200Doesnotapply
VOC 13.8 HAP 6.88E‐02 EPA
LiquidSoapAandBTanks
68S 68E NewConst. 396 3.3 8.58 5.6628 26,366VerticalFixed
RoofAboveground
Grey/Grey Yes 74SteamorHot
Water
DullesAirport,
WashingtonDC
1.20E‐01 8.71 200Doesnotapply
VOC 11.7 HAP 5.84E‐02 EPA
LiquidSoapAandBTanks
69S 69E NewConst. 396 3.3 8.58 5.6628 13,652VerticalFixed
RoofAboveground
Grey/Grey Yes 74SteamorHot
Water
DullesAirport,
WashingtonDC
1.20E‐01 8.71 200Doesnotapply
VOC 7.6 HAP 3.82E‐02 EPA
LiquidSoapAandBTanks
70S 70E NewConst. 396 3.3 8.58 5.6628 6,427VerticalFixed
RoofAboveground
Grey/Grey Yes 74SteamorHot
Water
DullesAirport,
WashingtonDC
1.20E‐01 8.71 200Doesnotapply
VOC 3.6 HAP 1.80E‐02 EPA
LiquidSoapAandBTanks
71S 71E NewConst. 396 3.3 8.58 5.6628 12,577VerticalFixed
RoofAboveground
Grey/Grey Yes 74SteamorHot
Water
DullesAirport,
WashingtonDC
1.20E‐01 8.71 200Doesnotapply
VOC 7.0 HAP 3.52E‐02 EPA
LiquidSoapAandBTanks
72S 72E NewConst. 396 3.3 8.58 5.6628 31,508VerticalFixed
RoofAboveground
Grey/Grey Yes 74SteamorHot
Water
DullesAirport,
WashingtonDC
1.20E‐01 8.71 200Doesnotapply
VOC 12.2 HAP 6.08E‐02 EPA
LiquidSoapAandBTanks
73S 73E NewConst. 396 3.3 8.58 5.6628 15,126VerticalFixed
RoofAboveground
Grey/Grey Yes 74SteamorHot
Water
DullesAirport,
WashingtonDC
1.20E‐01 8.71 200Doesnotapply
VOC 8.5 HAP 4.24E‐02 EPA
LiquidSoapAandBTanks
74S 74E NewConst. 396 3.3 8.58 5.6628 64,637VerticalFixed
RoofAboveground
Grey/Grey Yes 74SteamorHot
Water
DullesAirport,
WashingtonDC
1.20E‐01 8.71 200Doesnotapply
VOC 15.3 HAP 7.63E‐02 EPA
LiquidSoapAandBTanks
75S 75E NewConst. 396 3.3 8.58 5.6628 18,314VerticalFixed
RoofAboveground
Grey/Grey Yes 74SteamorHot
Water
DullesAirport,
WashingtonDC
1.20E‐01 8.71 200Doesnotapply
VOC 10.3 HAP 5.13E‐02 EPA
LiquidSoapAandBTanks
76S 76E NewConst. 396 3.3 8.58 5.6628 29,347VerticalFixed
RoofAboveground
Grey/Grey Yes 74SteamorHot
Water
DullesAirport,
WashingtonDC
1.20E‐01 8.71 200Doesnotapply
VOC 12.0 HAP 5.98E‐02 EPA
Page 4 of 16Trinity Consultants
141801.0078
Attachment LTabler Station
1 3 4 6 8 9A 9B 10A 13A 18 20 22A 22B 22C 27 38B 39C 39D 40
BulkStorageAreaName
TankEquipmentIdentificationNumber
EmissionPointIdentificationNumber
TypeofChange
Capacity(gallons)
InternalDiameter
(ft)
InternalHeight(ft)
MaxLiquidHeight
MaxAnnualThroughput(gal/yr)
TypeofTankShell
Color/RoofColor
AretheTanksHeated?
Providetheoperating
temperature(F)
Describehowheatisprovidedtothetank
City/StateforTANKS
calculations
MaxVaporPressure(psi)
LiquidDensity(lb/gal)
LiquidMolecularWeight
(lb/lb‐mol)
EmissionControlDevices
MaterialClassification
AnnualLoss
(lb/year)
MaterialClassificati
on
AnnualLoss
(lb/year)
EstimationMethod
41
AttachmentLEMISSIONSUNITDATASHEET‐STORAGETANKS
LiquidSoapAandBTanks
77S 77E NewConst. 396 3.3 8.58 5.6628 43,353VerticalFixed
RoofAboveground
Grey/Grey Yes 74SteamorHot
Water
DullesAirport,
WashingtonDC
1.20E‐01 8.71 200Doesnotapply
VOC 13.3 HAP 6.64E‐02 EPA
LiquidSoapAandBTanks
87S 87E NewConst. 1,585 5.3 13.78 9.0948 3,799,073VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.10E‐03 8.71 200Doesnotapply
VOC 3.5 HAP n/a EPA
LiquidSoapAandBTanks
88S 88E NewConst. 1,585 5.3 13.78 9.0948 3,799,073VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.10E‐03 8.71 200Doesnotapply
VOC 3.0 HAP n/a EPA
LiquidSoapAandBTanks
89S 89E NewConst. 1,585 5.3 13.78 9.0948 3,799,073VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.10E‐03 8.71 200Doesnotapply
VOC 3.0 HAP n/a EPA
LiquidSoapAandBTanks
90S 90E NewConst. 1,585 5.3 13.78 9.0948 3,799,073VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.10E‐03 8.71 200Doesnotapply
VOC 3.0 HAP n/a EPA
LiquidSoapAandBTanks
91S 91E NewConst. 1,585 5.3 13.78 9.0948 3,799,073VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.10E‐03 8.71 200Doesnotapply
VOC 3.0 HAP n/a EPA
LiquidSoapAandBTanks
92S 92E NewConst. 1,585 5.3 13.78 9.0948 3,799,073VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.10E‐03 8.71 200Doesnotapply
VOC 3.0 HAP n/a EPA
LiquidSoapAandBTanks
93S 93E NewConst. 1,585 5.3 13.78 9.0948 3,799,073VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.10E‐03 8.71 200Doesnotapply
VOC 3.0 HAP n/a EPA
LiquidSoapAandBTanks
94S 94E NewConst. 1,585 5.3 13.78 9.0948 3,799,073VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.10E‐03 8.71 200Doesnotapply
VOC 3.0 HAP n/a EPA
LiquidSoapAandBTanks
94bS 94bE NewConst. 1,585 5.3 13.78 9.0948 2,048,433VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.10E‐03 8.71 200Doesnotapply
VOC 2.0 HAP n/a EPA
LiquidSoapAandBTanks
94cS 94cE NewConst. 1,585 5.3 13.78 9.0948 2,048,433VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.10E‐03 8.71 200Doesnotapply
VOC 1.8 HAP n/a EPA
LiquidSoapAandBTanks
94dS 94dE NewConst. 1,585 5.3 13.78 9.0948 2,048,433VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.10E‐03 8.71 200Doesnotapply
VOC 1.8 HAP n/a EPA
LiquidSoapAandBTanks
94eS 94eE NewConst. 1,585 5.3 13.78 9.0948 2,048,433VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.10E‐03 8.71 200Doesnotapply
VOC 1.8 HAP n/a EPA
LiquidSoapAandBTanks
95S 95E NewConst. 1,585 5.3 13.78 9.0948 3,973,279VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.71E‐04 8.71 200Doesnotapply
VOC 5.67E‐01 HAP n/a EPA
LiquidSoapAandBTanks
96S 96E NewConst. 1,585 5.3 13.78 9.0948 3,973,279VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.71E‐04 8.71 200Doesnotapply
VOC 4.82E‐01 HAP n/a EPA
LiquidSoapAandBTanks
97S 97E NewConst. 1,585 5.3 13.78 9.0948 3,973,279VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.71E‐04 8.71 200Doesnotapply
VOC 4.82E‐01 HAP n/a EPA
LiquidSoapAandBTanks
98S 98E NewConst. 1,585 5.3 13.78 9.0948 3,973,279VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.71E‐04 8.71 200Doesnotapply
VOC 4.82E‐01 HAP n/a EPA
Page 5 of 16Trinity Consultants
141801.0078
Attachment LTabler Station
1 3 4 6 8 9A 9B 10A 13A 18 20 22A 22B 22C 27 38B 39C 39D 40
BulkStorageAreaName
TankEquipmentIdentificationNumber
EmissionPointIdentificationNumber
TypeofChange
Capacity(gallons)
InternalDiameter
(ft)
InternalHeight(ft)
MaxLiquidHeight
MaxAnnualThroughput(gal/yr)
TypeofTankShell
Color/RoofColor
AretheTanksHeated?
Providetheoperating
temperature(F)
Describehowheatisprovidedtothetank
City/StateforTANKS
calculations
MaxVaporPressure(psi)
LiquidDensity(lb/gal)
LiquidMolecularWeight
(lb/lb‐mol)
EmissionControlDevices
MaterialClassification
AnnualLoss
(lb/year)
MaterialClassificati
on
AnnualLoss
(lb/year)
EstimationMethod
41
AttachmentLEMISSIONSUNITDATASHEET‐STORAGETANKS
LiquidSoapAandBTanks
99S 99E NewConst. 1,585 5.3 13.78 9.0948 3,973,279VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.71E‐04 8.71 200Doesnotapply
VOC 4.82E‐01 HAP n/a EPA
LiquidSoapAandBTanks
100S 100E NewConst. 1,585 5.3 13.78 9.0948 3,973,279VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.71E‐04 8.71 200Doesnotapply
VOC 4.82E‐01 HAP n/a EPA
LiquidSoapAandBTanks
101S 101E NewConst. 1,585 5.3 13.78 9.0948 3,973,279VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.71E‐04 8.71 200Doesnotapply
VOC 4.82E‐01 HAP n/a EPA
LiquidSoapAandBTanks
102S 102E NewConst. 1,585 5.3 13.78 9.0948 3,973,279VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.71E‐04 8.71 200Doesnotapply
VOC 4.82E‐01 HAP n/a EPA
LiquidSoapAandBTanks
103S 103E NewConst. 1,585 5.3 13.78 9.0948 3,973,279VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.71E‐04 8.71 200Doesnotapply
VOC 4.82E‐01 HAP n/a EPA
LiquidSoapAandBTanks
104S 104E NewConst. 1,585 5.3 13.78 9.0948 3,973,279VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.71E‐04 8.71 200Doesnotapply
VOC 4.82E‐01 HAP n/a EPA
LiquidSoapAandBTanks
105S 105E NewConst. 1,585 5.3 13.78 9.0948 3,973,279VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.71E‐04 8.71 200Doesnotapply
VOC 4.82E‐01 HAP n/a EPA
LiquidSoapAandBTanks
106S 106E NewConst. 1,585 5.3 13.78 9.0948 3,973,279VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.71E‐04 8.71 200Doesnotapply
VOC 4.82E‐01 HAP n/a EPA
LiquidSoapAandBTanks
107S 107E NewConst. 1,585 5.3 13.78 9.0948 3,973,279VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.71E‐04 8.71 200Doesnotapply
VOC 4.82E‐01 HAP n/a EPA
LiquidSoapAandBTanks
108S 108E NewConst. 1,585 5.3 13.78 9.0948 3,973,279VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.71E‐04 8.71 200Doesnotapply
VOC 4.82E‐01 HAP n/a EPA
LiquidSoapAandBTanks
109S 109E NewConst. 1,585 5.3 13.78 9.0948 3,973,279VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.71E‐04 8.71 200Doesnotapply
VOC 4.82E‐01 HAP n/a EPA
LiquidSoapAandBTanks
110S 110E NewConst. 1,585 5.3 13.78 9.0948 3,973,279VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.71E‐04 8.71 200Doesnotapply
VOC 4.82E‐01 HAP n/a EPA
LiquidSoapAandBTanks
111S 111E NewConst. 1,585 5.3 13.78 9.0948 2,048,433VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.71E‐04 8.71 200Doesnotapply
VOC 3.18E‐01 HAP n/a EPA
LiquidSoapAandBTanks
112S 112E NewConst. 1,585 5.3 13.78 9.0948 2,048,433VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.71E‐04 8.71 200Doesnotapply
VOC 2.74E‐01 HAP n/a EPA
LiquidSoapAandBTanks
113S 113E NewConst. 1,585 5.3 13.78 9.0948 2,048,433VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.71E‐04 8.71 200Doesnotapply
VOC 2.74E‐01 HAP n/a EPA
LiquidSoapAandBTanks
114S 114E NewConst. 1,585 5.3 13.78 9.0948 2,048,433VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.71E‐04 8.71 200Doesnotapply
VOC 2.74E‐01 HAP n/a EPA
LiquidSoapAandBTanks
115S 115E NewConst. 1,585 5.3 13.78 9.0948 7,786VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.71E‐04 8.71 200Doesnotapply
VOC 6.05E‐03 HAP n/a EPA
Page 6 of 16Trinity Consultants
141801.0078
Attachment LTabler Station
1 3 4 6 8 9A 9B 10A 13A 18 20 22A 22B 22C 27 38B 39C 39D 40
BulkStorageAreaName
TankEquipmentIdentificationNumber
EmissionPointIdentificationNumber
TypeofChange
Capacity(gallons)
InternalDiameter
(ft)
InternalHeight(ft)
MaxLiquidHeight
MaxAnnualThroughput(gal/yr)
TypeofTankShell
Color/RoofColor
AretheTanksHeated?
Providetheoperating
temperature(F)
Describehowheatisprovidedtothetank
City/StateforTANKS
calculations
MaxVaporPressure(psi)
LiquidDensity(lb/gal)
LiquidMolecularWeight
(lb/lb‐mol)
EmissionControlDevices
MaterialClassification
AnnualLoss
(lb/year)
MaterialClassificati
on
AnnualLoss
(lb/year)
EstimationMethod
41
AttachmentLEMISSIONSUNITDATASHEET‐STORAGETANKS
LiquidSoapAandBTanks
116S 116E NewConst. 1,585 5.3 13.78 9.0948 7,786VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.71E‐04 8.71 200Doesnotapply
VOC 5.04E‐03 HAP n/a EPA
LiquidSoapAandBTanks
117S 117E NewConst. 1,585 5.3 13.78 9.0948 7,786VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.71E‐04 8.71 200Doesnotapply
VOC 5.04E‐03 HAP n/a EPA
LiquidSoapAandBTanks
118S 118E NewConst. 1,585 5.3 13.78 9.0948 7,786VerticalFixed
RoofAboveground
Grey/Grey Yes 90SteamorHot
Water
DullesAirport,
WashingtonDC
1.71E‐04 8.71 200Doesnotapply
VOC 5.04E‐03 HAP n/a EPA
DryConsumerLaundryand
CleaningProductsATanks
163S 132E NewConst. 42,879 13.5 36.1 23.8 39,447VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
0.50 8.81 200Doesnotapply
VOC 28.6 HAP n/a EPA
DryConsumerLaundryand
CleaningProductsATanks
164S 133E NewConst. 37,641 13.5 36.1 23.8 39,447VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
0.50 8.81 200Doesnotapply
VOC 28.6 HAP n/a EPA
DryConsumerLaundryand
CleaningProductsATanks
165S 134E NewConst. 6,809 7.9 18.4 12.1 39,447VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
0.50 8.81 200Doesnotapply
VOC 28.6 HAP 3.1 EPA
DryConsumerLaundryand
CleaningProductsATanks
166S 135E NewConst. 396 2.5 6.5 4.29 78,893VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
0.50 8.81 200Doesnotapply
VOC 47.1 HAP 2.36E‐01 EPA
DryConsumerLaundryand
CleaningProductsATanks
167S 136E NewConst. 396 2.5 6.5 4.29 78,893VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
0.50 8.81 200Doesnotapply
VOC 47.1 HAP 2.36E‐01 EPA
DryConsumerLaundryand
CleaningProductsATanks
168S 137E NewConst. 396 2.5 6.5 4.29 78,893VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
0.50 8.81 200Doesnotapply
VOC 47.1 HAP 2.36E‐01 EPA
DryConsumerLaundryand
CleaningProductsATanks
169S 138E NewConst. 181 2.3 6.0 3.96 39,447VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
0.50 8.81 200Doesnotapply
VOC 28.6 HAP 1.43E‐01 EPA
DryConsumerLaundryand
CleaningProductsATanks
170S 139E NewConst. 181 2.3 6.0 3.96 39,447VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
0.50 8.81 200Doesnotapply
VOC 28.6 HAP 1.43E‐01 EPA
DryConsumerLaundryand
CleaningProductsATanks
171S 140E NewConst. 181 2.3 6.0 3.96 39,447VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
0.50 8.81 200Doesnotapply
VOC 28.6 HAP 1.43E‐01 EPA
DryConsumerLaundryand
CleaningProductsATanks
172S 141E NewConst. 181 2.3 6.0 3.96 39,447VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
0.50 8.81 200Doesnotapply
VOC 28.6 HAP 1.43E‐01 EPA
DryConsumerLaundryand
CleaningProductsATanks
173S 142E NewConst. 181 2.3 6.0 3.96 39,447VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
0.50 8.81 200Doesnotapply
VOC 28.6 HAP 1.43E‐01 EPA
DryConsumerLaundryand
CleaningProductsATanks
174S 143E NewConst. 181 2.3 6.0 3.96 39,447VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
0.50 8.81 200Doesnotapply
VOC 28.6 HAP 1.43E‐01 EPA
DryConsumerLaundryand
CleaningProductsATanks
175S 144E NewConst. 181 2.3 6.0 3.96 39,447VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
0.50 8.81 200Doesnotapply
VOC 28.6 HAP 1.43E‐01 EPA
Page 7 of 16Trinity Consultants
141801.0078
Attachment LTabler Station
1 3 4 6 8 9A 9B 10A 13A 18 20 22A 22B 22C 27 38B 39C 39D 40
BulkStorageAreaName
TankEquipmentIdentificationNumber
EmissionPointIdentificationNumber
TypeofChange
Capacity(gallons)
InternalDiameter
(ft)
InternalHeight(ft)
MaxLiquidHeight
MaxAnnualThroughput(gal/yr)
TypeofTankShell
Color/RoofColor
AretheTanksHeated?
Providetheoperating
temperature(F)
Describehowheatisprovidedtothetank
City/StateforTANKS
calculations
MaxVaporPressure(psi)
LiquidDensity(lb/gal)
LiquidMolecularWeight
(lb/lb‐mol)
EmissionControlDevices
MaterialClassification
AnnualLoss
(lb/year)
MaterialClassificati
on
AnnualLoss
(lb/year)
EstimationMethod
41
AttachmentLEMISSIONSUNITDATASHEET‐STORAGETANKS
DryConsumerLaundryand
CleaningProductsATanks
176S 145E NewConst. 181 2.3 6.0 3.96 39,447VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
0.50 8.81 200Doesnotapply
VOC 28.6 HAP 1.43E‐01 EPA
DryConsumerLaundryand
CleaningProductsATanks
177S 146E NewConst. 181 2.3 6.0 3.96 39,447VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
0.50 8.81 200Doesnotapply
VOC 28.6 HAP 1.43E‐01 EPA
DryConsumerLaundryand
CleaningProductsATanks
178S 147E NewConst. 181 2.3 6.0 3.96 39,447VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
0.50 8.81 200Doesnotapply
VOC 28.6 HAP 1.43E‐01 EPA
DryConsumerLaundryand
CleaningProductsATanks
179S 148E NewConst. 181 2.3 6.0 3.96 39,447VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
0.50 8.81 200Doesnotapply
VOC 28.6 HAP 1.43E‐01 EPA
DryConsumerLaundryand
CleaningProductsATanks
180S 149E NewConst. 181 2.3 6.0 3.96 39,447VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
0.50 8.81 200Doesnotapply
VOC 28.6 HAP 1.43E‐01 EPA
DryConsumerLaundryand
CleaningProductsATanks
181S 150E NewConst. 181 2.3 6.0 3.96 39,447VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
0.50 8.81 200Doesnotapply
VOC 28.6 HAP 1.43E‐01 EPA
DryConsumerLaundryand
CleaningProductsATanks
182S 151E NewConst. 181 2.3 6.0 3.96 39,447VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
0.50 8.81 200Doesnotapply
VOC 28.6 HAP 1.43E‐01 EPA
DryConsumerLaundryand
CleaningProductsATanks
183S 152E NewConst. 181 2.3 6.0 3.96 39,447VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
0.50 8.81 200Doesnotapply
VOC 28.6 HAP 1.43E‐01 EPA
DryConsumerLaundryand
CleaningProductsATanks
184S 153E NewConst. 181 2.3 6.0 3.96 39,447VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
0.50 8.81 200Doesnotapply
VOC 28.6 HAP 1.43E‐01 EPA
DryConsumerLaundryand
CleaningProductsATanks
185S 154E NewConst. 181 2.3 6.0 3.96 39,447VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
0.50 8.81 200Doesnotapply
VOC 28.6 HAP 1.43E‐01 EPA
DryConsumerLaundryand
CleaningProductsATanks
186S 155E NewConst. 181 2.3 6.0 3.96 39,447VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
0.50 8.81 200Doesnotapply
VOC 28.6 HAP 1.43E‐01 EPA
DryConsumerLaundryand
CleaningProductsATanks
187S 156E NewConst. 181 2.3 6.0 3.96 39,447VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
0.50 8.81 200Doesnotapply
VOC 28.6 HAP 1.43E‐01 EPA
DryConsumerLaundryand
CleaningProductsATanks
188S 157E NewConst. 181 2.3 6.0 3.96 39,447VerticalFixed
RoofAboveground
Grey/Grey Yes 77SteamorHot
Water
DullesAirport,
WashingtonDC
0.50 8.81 200Doesnotapply
VOC 28.6 HAP 1.43E‐01 EPA
FuelTanks 208S 177E NewConst. 5,162 8.0 20.8 13.73 70,000VerticalFixed
RoofAboveground
Grey/Grey No Ambient N/A
DullesAirport,
WashingtonDC
2.20E‐02 7.1 130Doesnotapply
VOC 4.6 HAP n/a EPA
Page 8 of 16Trinity Consultants
141801.0078
Attachment LTabler Station
Number: Question: Notes:Sheetversion:
0 IdentificationNumber
1 LoadingAreaName
2TypeofCargoVessels
AccommodatedatthisTransferPoint
Choose:Drums,MarineVessels,RailTankCars,andTankTrucks
7ProjectedMaximumOperating
ScheduleBulkLiquidDataLiquidName PAM Surfactant SulfuricAcidAnnualthroughput(Mgal/yr) 150 15,000 2,000Max.BulkLiquidTemp(F) 69 69 69Truevaporpressure(psia) 1.69E‐03 1.50E‐03 1.69E‐03Filltype Submerged Submerged SubmergedVOCEmissionRate(lb/yr) 3.5E‐01 60.1 ‐‐H2SO4EmissionRate(lb/yr) 1.1E‐01 ‐‐ 4.7ControlEquipment N/A N/A N/A
RailTankCarsandTankTrucks
24/7/365
8
AttachmentLEMISSIONSUNITDATASHEET‐BULKLIQUIDTRANSFEROPERATIONS
Response:BulkLiquidTransfer
19S
SurfactantBulkLiquidTransfer
Page 9 of 16Trinity Consultants
141801.0078
Attachment LTabler Station
Utilities‐Road‐ConstantsParameter Value UnitIndustrialaugmentationfactor 1 dimensionlessNumberoftrafficlanes 2Surfacematerialsiltcontent1 3.3% %Surfacedustloading 125 lb/mile
Utilities‐Road‐Parameters
DescriptionAverage Weight2
MilesperTrip2
MaximumTripsperHour
Maximum Trips per
YearControl
Device IDControl
Efficiency(tons) %
DeliveryTrucks 40 0.04167 30.8 365 -- --EmployeeVehicles 2 0.04167 0.5 365 -- --
Utilities‐Road‐Emissions
(lb/hr) (tpy) (lb/hr) (tpy)DeliveryTrucks 5.0E‐04 2.2E‐03 -- --EmployeeVehicles 1.0E‐06 4.4E‐06 -- --
TOTAL 5.0E‐04 2.2E‐03 -- --
2.ConservativeassumptionbasedonProcterandGambledesigndata.
AttachmentLEMISSIONSUNITDATASHEET‐PAVEDHAULROADS
3.FromEmissionFactorDocumentationforAP‐42Section13.2.1,PavedRoads, Equation2‐2,assitedinWVDEPR‐13PermitFormAttachmentLforHaulRoads
PollutantUncontrolledTSPEmissions3 ControlledTSPEmissions
1.ConservativelyassumedtobeequaltoaveragefactorforAsphaltBatching,AP‐42Section13.2.1PavedRoads ,Table13.2.1‐3
Page 10 of 16Trinity Consultants
141801.0078
Attachment LTabler Station
Number: Question: Response: Notes:Sheetversion: IndirectHeatExchanger
0 ControlDeviceIDNo. 165Eand166E1 Manufacturer Cleaver‐Brooks
2ModelNumber:SerialNumber:
TBD
3 NumberofUnits 24 Use Plantsteam7 DateConstructed November2016
9Maximumdesignheatinputperunit 62 MMBtu/hr
10 Peakheatinputperunit
11Steamproducedatmaximumdesign
output 50,267each pph12 ProjectedOperatingSchedule 24/7/365
13TypeofFiringEquipmenttobeUsed
NaturalGasBurners Choosefrompulverizedcoal,spreaderstoker,oilburners,naturalgasburners,orother.
Fuel NaturalGasQuantityofFuelUsed(ft3/hr) 62,000eachQuantityofFuelUsedAnnually
(MMft3/hr) 4,757,731each
BTUContent(BTU/ft3) 1,000Emissionsaftercontrol(lb/hr)
CO 4.6NOX 9.0Pb 1.2E‐04PM10 9.3E‐01
SO2 7.4E‐02VOC 4.5E‐01
AttachmentLEMISSIONSUNITDATASHEET‐INDIRECTHEATEXCHANGER
25
38
Page 11 of 16Trinity Consultants
141801.0078
Attachment LTabler Station
Number: Question: Response: Notes:Sheetversion: IndirectHeatExchanger
0 ControlDeviceIDNo. 167E1 Manufacturer Cleaver‐Brooks
2ModelNumber:SerialNumber:
TBD
3 NumberofUnits 14 Use Plantsteam7 DateConstructed November2016
9Maximumdesignheatinputperunit 31 MMBtu/hr
10 Peakheatinputperunit
11Steamproducedatmaximumdesign
output 25,134 pph12 ProjectedOperatingSchedule 24/7/365
13TypeofFiringEquipmenttobeUsed
NaturalGasBurnersChoosefrompulverizedcoal,spreaderstoker,oilburners,naturalgasburners,orother.
Fuel NaturalGasQuantityofFuelUsed(ft3/hr) 31,000QuantityofFuelUsedAnnually
(MMft3/hr) 2,378,866
BTUContent(BTU/ft3) 1,000Emissionsaftercontrol(lb/hr)
CO 1.1NOX 2.3Pb 1.5E‐05PM10 2.3E‐01
SO2 1.9E‐02VOC 1.1E‐01
AttachmentLEMISSIONSUNITDATASHEET‐INDIRECTHEATEXCHANGER
25
38
Page 12 of 16Trinity Consultants
141801.0078
Attachment LTabler Station
Number: Question: Response: Notes:Sheetversion: IndirectHeatExchanger
0 ControlDeviceIDNo. 168E1 Manufacturer Cleaver‐Brooks
2ModelNumber:SerialNumber:
TBD
3 NumberofUnits 14 Use Plantsteam7 DateConstructed November2016
9Maximumdesignheatinputperunit 11 MMBtu/hr
10 Peakheatinputperunit
11Steamproducedatmaximumdesign
output 8,918 pph12 ProjectedOperatingSchedule AsNeeded
13TypeofFiringEquipmenttobeUsed
NaturalGasBurnersChoosefrompulverizedcoal,spreaderstoker,oilburners,naturalgasburners,orother.
Fuel NaturalGasQuantityofFuelUsed(ft3/hr) 11,000QuantityofFuelUsedAnnually
(MMft3/hr) 844,114
BTUContent(BTU/ft3) 1,000
AttachmentLEMISSIONSUNITDATASHEET‐INDIRECTHEATEXCHANGER
25
Page 13 of 16Trinity Consultants
141801.0078
Attachment LTabler Station
REVISED
Number: Question: Response: Notes:Sheetversion: General
0 IdentificationNumber 1Sand2S asassignedonEquipmentListForm
1Nameortypeandmodelofproposed
affectedsourceSurfactantMakingProcess
4Namesandmaximumamountof
proposedprocessmaterialsproducedperhour
6,000gal/hr gal/hroffinishedproduct
5Givechemicalreactions,ifapplicable,thatwillbeinvolvedinthegeneration
ofairpollutants
1.CombustionofliquidStoSO2'2.OxidationofSO2toSO3
2.SO3reactedwithorganicfattyalcohol
6 CombustiondataSulfurwillbeburned.Naturalgas
burnedduringstartup7 Projectedoperatingschedule 24/7/365
Pollutant NOXEmissionRate(lb/hr) 1.8
Pollutant COEmissionRate(lb/hr) 0.1
Pollutant SO2EmissionRate(lb/hr) 2.1
Pollutant VOCEmissionRate(lb/hr) 1.9
Pollutant PM10
EmissionRate(lb/hr) 7.0Pollutant CO
EmissionRate(lb/hr) 1.3
Pollutant H2SO4EmissionRate(lb/hr) 5.1EmissionRate(lb/hr) Lead
Pollutant 7.8E‐06Pollutant HAP
EmissionRate(lb/hr) 3.0E‐02
9Recordkeeping
NSPSVVa:Recordkeepingtoshowthatfacilityisexempt.
Number: Question: Response: Notes:Sheetversion: General
0 IdentificationNumber 119S asassignedonEquipmentListForm
1Nameortypeandmodelofproposed
affectedsourceLiquidSoapAandBPacking/Filling
4Namesandmaximumamountof
proposedprocessmaterialsproducedperhour
15,959 gal/houroffinishedproduct
5Givechemicalreactions,ifapplicable,thatwillbeinvolvedinthegeneration
ofairpollutants N/A7 Projectedoperatingschedule 24/7/365
Pollutant VOCEmissionRate(lb/hr) 2.5E‐04
AttachmentLEMISSIONSUNITDATASHEET‐GENERAL
8
AttachmentLEMISSIONSUNITDATASHEET‐GENERAL
8
Page 14 of 16Trinity Consultants
141801.0078
Attachment LTabler Station
REVISED
Number: Question: Response: Notes:Sheetversion: General
0 IdentificationNumber 195S asassignedonEquipmentListForm
1Nameortypeandmodelofproposed
affectedsourceDryConsumerLaundryandCleaning
ProductsAAdditive1
4Namesandmaximumamountof
proposedprocessmaterialsproducedperhour
393,701 ft/hroffinishedproduct
5Givechemicalreactions,ifapplicable,thatwillbeinvolvedinthegeneration
ofairpollutants N/A7 Projectedoperatingschedule 24/7/365
Pollutant VOCEmissionRate(lb/hr) 2.0
Number: Question: Response: Notes:Sheetversion: General
0 IdentificationNumber 216S asassignedonEquipmentListForm
1Nameortypeandmodelofproposed
affectedsourceWaterPretreatmentChemicals
4Namesandmaximumamountof
proposedprocessmaterialsproducedperhour
44lb/hr(ofmaterialsthatcontainVOCand/or
HAP)
5Givechemicalreactions,ifapplicable,thatwillbeinvolvedinthegeneration
ofairpollutantsN/A
7 Projectedoperatingschedule 24/7/365Pollutant VOC
EmissionRate(lb/hr) 3.0Pollutant HAP
EmissionRate(lb/hr) 9.1E‐04
Number: Question: Response: Notes:Sheetversion: General
0 IdentificationNumber 247S asassignedonEquipmentListForm
1Nameortypeandmodelofproposed
affectedsourceForming
4Namesandmaximumamountof
proposedprocessmaterialsproducedperhour
100,000 tons/year
5Givechemicalreactions,ifapplicable,thatwillbeinvolvedinthegeneration
ofairpollutants N/A7 Projectedoperatingschedule 24/7/365
Pollutant VOCEmissionRate(lb/hr) 7.0E‐01
Number: Question: Response: Notes:Sheetversion: General
0 IdentificationNumber 248S asassignedonEquipmentListForm
1Nameortypeandmodelofproposed
affectedsourcePartsWashing/ProcessCleaning
4Namesandmaximumamountof
proposedprocessmaterialsproducedperhour
6 tons/year
5Givechemicalreactions,ifapplicable,thatwillbeinvolvedinthegeneration
ofairpollutantsN/A
7 Projectedoperatingschedule 24/7/365Pollutant VOC
EmissionRate(lb/hr) 1.4
EMISSIONSUNITDATASHEET‐GENERAL
8
EMISSIONSUNITDATASHEET‐GENERAL
8
AttachmentL
AttachmentL
EMISSIONSUNITDATASHEET‐GENERALAttachmentL
AttachmentLEMISSIONSUNITDATASHEET‐GENERAL
8
8
Page 15 of 16Trinity Consultants
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Attachment LTabler Station
REVISED
Number: Question: Response: Notes:Sheetversion: General
0 IdentificationNumber 257S asassignedonEquipmentListForm
1Nameortypeandmodelofproposed
affectedsourcePrintingInk
4Namesandmaximumamountof
proposedprocessmaterialsproducedperhour
0.39lb/hrlb/hr(ofmaterialsthatcontainVOCand/or
HAP)
5Givechemicalreactions,ifapplicable,thatwillbeinvolvedinthegeneration
ofairpollutantsN/A
7 Projectedoperatingschedule 24/7/365Pollutant VOC
EmissionRate(lb/hr) 8.65E‐02Pollutant HAP
EmissionRate(lb/hr) 3.7E‐02
Number: Question: Response: Notes:Sheetversion: General
0 IdentificationNumber 258S asassignedonEquipmentListForm
1Nameortypeandmodelofproposed
affectedsourceCasePackingGlue
4Namesandmaximumamountof
proposedprocessmaterialsproducedperhour
79lb/hrlb/hr(ofmaterialsthatcontainVOCand/or
HAP)
5Givechemicalreactions,ifapplicable,thatwillbeinvolvedinthegeneration
ofairpollutantsN/A
7 Projectedoperatingschedule 24/7/365Pollutant VOC
EmissionRate(lb/hr) 4.73E‐02Pollutant HAP
EmissionRate(lb/hr) 1.6E‐03
EMISSIONSUNITDATASHEET‐GENERAL
8
AttachmentLEMISSIONSUNITDATASHEET‐GENERAL
8
AttachmentL
Page 16 of 16Trinity Consultants
141801.0078
P&G – Tabler Station | R13 Permit Trinity Consultants
ATTACHMENT M
Air Pollution Control Device Sheet
Attachment MTabler Station
Number: Question: Response: Notes:Sheetversion: WetCollectingSystem‐Scrubber
EquipmentDescription SurfactantMakingProcess0 ControlDeviceIDNo.: 1C MustmatchEmissionUnitsTable
2 Method: PackedBedChoices:Packedbed,spraytower,mechanical,venturi,
cycle,orifice,other(specify)10 ScrubbingLiquor: Water Compositionandweight%13 Pressuredropthroughscrubber: ~6 inchesH2O15 Liquorflowratestoscrubber: ~572 Designmaximum,gal/min23 Gasflowrate: ~14,000scfm Designmaximum,acfm26 Typeofpollutant(s)Controlled SOx ChooseSOx,Odor,Particulate,Other
Number: Question: Response: Notes:Sheetversion: WetCollectingSystem‐Scrubber
EquipmentDescription SurfactantMakingProcess0 ControlDeviceIDNo.: 2C MustmatchEmissionUnitsTable
2 Method: PackedBedChoices:Packedbed,spraytower,mechanical,venturi,
cycle,orifice,other(specify)10 ScrubbingLiquor: Water Compositionandweight%13 Pressuredropthroughscrubber: ~6 inchesH2O15 Liquorflowratestoscrubber: ~572 Designmaximum,gal/min23 Gasflowrate: ~14,000scfm Designmaximum,acfm26 Typeofpollutant(s)Controlled SOx ChooseSOx,Odor,Particulate,Other
Number: Question: Response: Notes:Sheetversion: MechanicalCollector‐Cyclone
EquipmentDescription Rotoclone0 ControlDeviceIDNo.: 3C MustmatchEmissionUnitsTable
2 Method: WetChoices:Wet,Single‐stage,dry,multiple(number?),in
series(number)5 PressureDrop(inH2O) ~11.29 Guaranteedcollectionefficiency: 96% Alsoincludeminimum%13 Totalflowrate ~3000acfm15 GasFlowRateintoCollector ~2250scfm
Number: Question: Response: Notes:Sheetversion: MechanicalCollector‐Cyclone
EquipmentDescription Rotoclone0 ControlDeviceIDNo.: 4C MustmatchEmissionUnitsTable
2 Method: WetChoices:Wet,Single‐stage,dry,multiple(number?),in
series(number)5 PressureDrop(inH2O) ~11.29 Guaranteedcollectionefficiency: 96% Alsoincludeminimum%13 Totalflowrate ~3000acfm15 GasFlowRateintoCollector ~4750scfm
Number: Question: Response: Notes:Sheetversion: MechanicalCollector‐Cyclone
EquipmentDescription Rotoclone0 ControlDeviceIDNo.: 5C MustmatchEmissionUnitsTable
2 Method: WetChoices:Wet,Single‐stage,dry,multiple(number?),in
series(number)5 PressureDrop(inH2O) ~10.49 Guaranteedcollectionefficiency: 96% Alsoincludeminimum%13 Totalflowrate ~3000acfm15 GasFlowRateintoCollector ~4750scfm
Number: Question: Response: Notes:Sheetversion: MechanicalCollector‐Cyclone
EquipmentDescription Rotoclone0 ControlDeviceIDNo.: 6C MustmatchEmissionUnitsTable
2 Method: WetChoices:Wet,Single‐stage,dry,multiple(number?),in
series(number)5 PressureDrop(inH2O) ~11.29 Guaranteedcollectionefficiency: 96% Alsoincludeminimum%13 Totalflowrate ~3000acfm15 GasFlowRateintoCollector ~3150scfm
Number: Question: Response: Notes:Sheetversion: MechanicalCollector‐Cyclone
EquipmentDescription Rotoclone0 ControlDeviceIDNo.: 7C MustmatchEmissionUnitsTable
2 Method: WetChoices:Wet,Single‐stage,dry,multiple(number?),in
series(number)5 PressureDrop(inH2O) ~11.29 Guaranteedcollectionefficiency: 96% Alsoincludeminimum%13 Totalflowrate ~9600acfm15 GasFlowRateintoCollector ~1000scfm
Number: Question: Response: Notes:Sheetversion: MechanicalCollector‐Cyclone
EquipmentDescription Rotoclone0 ControlDeviceIDNo.: 8C MustmatchEmissionUnitsTable
2 Method: WetChoices:Wet,Single‐stage,dry,multiple(number?),in
series(number)5 PressureDrop(inH2O) ~11.29 Guaranteedcollectionefficiency: 96% Alsoincludeminimum%13 Totalflowrate ~9600acfm15 GasFlowRateintoCollector ~1000scfm
Number: Question: Response: Notes:Sheetversion: MechanicalCollector‐Cyclone
EquipmentDescription Rotoclone0 ControlDeviceIDNo.: 9C MustmatchEmissionUnitsTable5 PressureDrop(inH2O) ~11.2
2 Method: WetChoices:Wet,Single‐stage,dry,multiple(number?),in
series(number)9 Guaranteedcollectionefficiency: 98% Alsoincludeminimum%13 Totalflowrate ~5500acfm15 GasFlowRateintoCollector ~1750scfm
Number: Question: Response: Notes:Sheetversion: MechanicalCollector‐Cyclone
EquipmentDescription Rotoclone0 ControlDeviceIDNo.: 10C MustmatchEmissionUnitsTable
2 Method: WetChoices:Wet,Single‐stage,dry,multiple(number?),in
series(number)5 PressureDrop(inH2O) ~11.29 Guaranteedcollectionefficiency: 98% Alsoincludeminimum%13 Totalflowrate ~5500acfm15 GasFlowRateintoCollector ~1750scfm
Number: Question: Response: Notes:Sheetversion: MechanicalCollector‐Cyclone
EquipmentDescription Rotoclone0 ControlDeviceIDNo.: 11C MustmatchEmissionUnitsTable
2 Method: WetChoices:Wet,Single‐stage,dry,multiple(number?),in
series(number)5 PressureDrop(inH2O) ~11.29 Guaranteedcollectionefficiency: 98% Alsoincludeminimum%13 Totalflowrate ~5500acfm15 GasFlowRateintoCollector ~1750scfm
AttachmentMAIRPOLLUTIONCONTROLDEVICESHEET
Page 1 of 2Trinity Consultants
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Attachment MTabler Station
AttachmentMAIRPOLLUTIONCONTROLDEVICESHEET
Number: Question: Response: Notes:Sheetversion: MechanicalCollector‐Cyclone
EquipmentDescription Rotoclones0 ControlDeviceIDNo.: 12C MustmatchEmissionUnitsTable
2 Method: WetChoices:Wet,Single‐stage,dry,multiple(number?),in
series(number)5 PressureDrop(inH2O) ~5.29 Guaranteedcollectionefficiency: 98% Alsoincludeminimum%13 Totalflowrate ~5500acfm15 GasFlowRateintoCollector ~3050scfm
Number: Question: Response: Notes:Sheetversion: MechanicalCollector‐Cyclone
EquipmentDescription Rotoclone0 ControlDeviceIDNo.: 13C MustmatchEmissionUnitsTable
2 Method: WetChoices:Wet,Single‐stage,dry,multiple(number?),in
series(number)5 PressureDrop(inH2O) ~9.29 Guaranteedcollectionefficiency: 96% Alsoincludeminimum%13 Totalflowrate ~5900acfm15 GasFlowRateintoCollector ~1400scfm
Number: Question: Response: Notes:Sheetversion: Flaresystem
EquipmentDescription RegenerativeThermalOxidizer0 ControlDeviceIDNo.: 14C MustmatchEmissionUnitsTable5 Maxcapacityofflare: 75 scf/min7 Estimatedcombustionefficiency: 97% Estimated%8 FuelUsed NaturalGas9 BurnerRating ~2MMBtu/hr
30 Maximummassflowrateofwastegas: ~6146 scf.Estimatedtotalcombustibletoflare.
31Estimatedtotalflowratetoflareincluding
materialtobeburned,carriergases,auxiliaryfuel,etc.:
~158.6 lb/hr
Temperatureofemissionstream(inlet) ~104‐184 DegreesF
Temperatureofemissionstream(outlet) ~1500 DegreesF
Number: Question: Response: Notes:Sheetversion: Baghouse
EquipmentDescription BinVentFilter0 ControldeviceIDNo.: 15C MustmatchEmissionUnitsTable16 Gasflowrateintocollector: ~400scfm ACFM21 ParticulateLoading(outlet): ~0.02 grain/scf
Number: Question: Response: Notes:Sheetversion: Baghouse
EquipmentDescription Baghouse0 ControldeviceIDNo.: 16C MustmatchEmissionUnitsTable16 Gasflowrateintocollector: ~275scfm ACFM21 ParticulateLoading(outlet): ~0.02 grain/scf
Number: Question: Response: Notes:Sheetversion: Baghouse
EquipmentDescription Baghouse0 ControldeviceIDNo.: 17C MustmatchEmissionUnitsTable16 Gasflowrateintocollector: ~260scfm ACFM21 ParticulateLoading(outlet): ~0.02 grain/scf
Number: Question: Response: Notes:Sheetversion: Baghouse
EquipmentDescription Baghouse0 ControldeviceIDNo.: 18C MustmatchEmissionUnitsTable16 Gasflowrateintocollector: ~18000scfm ACFM21 ParticulateLoading(outlet): ~0.01 grain/scf
Number: Question: Response: Notes:Sheetversion: Baghouse
EquipmentDescription Baghouse0 ControldeviceIDNo.: 19C MustmatchEmissionUnitsTable16 Gasflowrateintocollector: ~18000scfm ACFM21 ParticulateLoading(outlet): ~0.01 grain/scf
Number: Question: Response: Notes:Sheetversion: Baghouse
EquipmentDescription Baghouse0 ControldeviceIDNo.: 20C MustmatchEmissionUnitsTable16 Gasflowrateintocollector: ~6500scfm ACFM21 ParticulateLoading(outlet): ~0.01 grain/scf
Number: Question: Response: Notes:Sheetversion: MechanicalCollector‐Cyclone
EquipmentDescription Cyclone0 ControlDeviceIDNo.: 21C MustmatchEmissionUnitsTable
2 Method: DryChoices:Wet,Single‐stage,dry,multiple(number?),in
series(number)9 Guaranteedcollectionefficiency: 90% Alsoincludeminimum%13 Totalflowrate ~1298cfm
Number: Question: Response: Notes:Sheetversion: MechanicalCollector‐Cyclone
EquipmentDescription Cyclone0 ControlDeviceIDNo.: 22C MustmatchEmissionUnitsTable
2 Method: DryChoices:Wet,Single‐stage,dry,multiple(number?),in
series(number)9 Guaranteedcollectionefficiency: 90% Alsoincludeminimum%13 Totalflowrate ~1298cfm
Number: Question: Response: Notes:Sheetversion: MechanicalCollector‐Cyclone
EquipmentDescription Cyclone0 ControlDeviceIDNo.: 23C MustmatchEmissionUnitsTable
2 Method: DryChoices:Wet,Single‐stage,dry,multiple(number?),in
series(number)9 Guaranteedcollectionefficiency: 90% Alsoincludeminimum%13 Totalflowrate ~1298cfm
Number: Question: Response: Notes:Sheetversion: MechanicalCollector‐Cyclone
EquipmentDescription Cyclone0 ControlDeviceIDNo.: 24C MustmatchEmissionUnitsTable
2 Method: DryChoices:Wet,Single‐stage,dry,multiple(number?),in
series(number)9 Guaranteedcollectionefficiency: 90% Alsoincludeminimum%13 Totalflowrate ~1298cfm
Number: Question: Response: Notes:Sheetversion: MechanicalCollector‐Cyclone
EquipmentDescription Cyclone0 ControlDeviceIDNo.: 25C MustmatchEmissionUnitsTable
2 Method: DryChoices:Wet,Single‐stage,dry,multiple(number?),in
series(number)9 Guaranteedcollectionefficiency: 90% Alsoincludeminimum%13 Totalflowrate ~1298cfm
Number: Question: Response: Notes:Sheetversion: Baghouse
EquipmentDescription BinVentFilter0 ControldeviceIDNo.: 26C MustmatchEmissionUnitsTable16 Gasflowrateintocollector: TBD ACFM21 ParticulateLoading(outlet): TBD grain/scf
33
Page 2 of 2Trinity Consultants
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P&G – Tabler Station | R13 Permit Trinity Consultants
ATTACHMENT N
Supporting Emission Calculations
Attachment NTabler Station
TableN‐0a.EmissionsSummary
BusinessUnit/Process PM PM10 PM2.5 VOC HAPs NOx CO SO2 H2SO4Chemicals 23.6 23.6 23.6 5.5 9.2E‐02 4.7 2.9E‐01 1.6 19.4
Tanks ‐‐ ‐‐ ‐‐ 1.2 9.1E‐02 ‐‐ ‐‐ ‐‐ 1.5E‐03TruckLoading ‐‐ ‐‐ ‐‐ 5.2E‐02 ‐‐ ‐‐ ‐‐ ‐‐ 2.4E‐03SO2Scrubber 23.6 23.6 23.6 4.2 1.1E‐03 4.7 2.9E‐01 1.6 19.4
SoapMakingA&B 20.0 20.0 20.0 44.1 3.4E‐02 1.1 5.8 6.2E‐03 0.0Tanks ‐‐ ‐‐ ‐‐ 2.6 3.4E‐02 ‐‐ ‐‐ ‐‐ ‐‐RTO 6.5E‐02 6.5E‐02 6.5E‐02 8.0 5.2E‐06 1.1 5.8 6.2E‐03 ‐‐
DustControl 20.0 20.0 20.0 33.4 ‐‐ ‐‐ ‐‐ ‐‐ ‐‐Packing/Filling ‐‐ ‐‐ ‐‐ 1.11E‐03 ‐‐ ‐‐ ‐‐ ‐‐ ‐‐
DryConsumerProductsA 16.7 16.7 16.7 9.3 3.3E‐03 0.0 0.0 0.0 0.0Tanks ‐‐ ‐‐ ‐‐ 0.7 3.3E‐03 ‐‐ ‐‐ ‐‐ ‐‐
Converting 16.7 16.7 16.7 ‐‐ ‐‐ ‐‐ ‐‐ ‐‐ ‐‐Additive ‐‐ ‐‐ ‐‐ 8.7 ‐‐ ‐‐ ‐‐ ‐‐ ‐‐
Utilities 7.2 9.7 9.7 16.0 1.4 56.9 32.4 4.6E‐01 4.9E‐03Boilers 2.6 5.1 5.1 2.4 1.3E+00 49.4 25.1 4.1E‐01 4.4E‐03Engines 7.0E‐02 6.9E‐02 6.9E‐02 6.7E‐02 2.3E‐02 3.5 0.7 1.6E‐03 ‐‐
CoolingTowers 3.9 3.9 3.9 ‐‐ ‐‐ ‐‐ ‐‐ ‐‐ ‐‐Heaters 6.0E‐01 6.0E‐01 6.0E‐01 4.3E‐01 1.5E‐01 3.9 6.6 4.7E‐02 5.1E‐04
FuelTanks ‐‐ ‐‐ ‐‐ 2.3E‐03 ‐‐ ‐‐ ‐‐ ‐‐ ‐‐WaterTreatmentChemicals ‐‐ ‐‐ ‐‐ 13.0 4.0E‐03 ‐‐ ‐‐ ‐‐ ‐‐
AuxiliaryActivities 5.8E+00 5.8E+00 5.8E+00 10.11 2.99E‐01 3.8E+00 6.3E+00 4.4E‐02 4.7E‐04GlueUsage ‐‐ ‐‐ ‐‐ 2.07E‐01 6.90E‐03 ‐‐ ‐‐ ‐‐ ‐‐Printing ‐‐ ‐‐ ‐‐ 3.79E‐01 1.60E‐01 ‐‐ ‐‐ ‐‐ ‐‐
PavedRoads 2.2E‐03 ‐‐ ‐‐ ‐‐ ‐‐ ‐‐ ‐‐ ‐‐ ‐‐PlasticsMolding 5.80 5.80 5.80 9.52 1.3E‐01 3.75 6.34 4.4E‐02 4.7E‐04
Total 73.3 75.8 75.8 84.9 1.9 66.4 44.8 2.2 19.4
PotentialtoEmit(tpy)
Page 1 of 42Trinity Consultants
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Attachment NTabler Station
TableN‐0b.HAP‐EmissionsSummary
HAPEmissions Hexane EthyleneOxide Formaldehyde VinylAcetate 1,4Dioxane HydrogenChloride Acetophenone Propylene Chloroform Lead GlycolEther OtherCombustionHAP1
Total(tpy) 1.46 4.8E‐02 6.0E‐02 6.9E‐03 5.4E‐02 1.8E‐02 7.9E‐05 9.2E‐03 4.0E‐03 4.1E‐04 1.7E‐01 2.1E‐02
PotentialtoEmit
1.Includes:2‐methylnaphthalene,3‐methylchloranthrene,7,12‐Dimethylbenz(a)anthracene,acetaldehyde,acenaphthene,acenaphthylene,acrolein,anthracene,benz(a)anthracene,benzene,benzo(a)pyrene,bezo(b)fluoranthene,benzo(g,h,i)perylene,benzo(k)fluoranthene,chrysene,dibenzo(a,h)anthracene,dichlorobenzene,ethylbenzene,fluoranthene,fluorene,indeno(1,2,3‐cd)pyrene,naphthalene,OCDD,PAH,phenanathrene,pyrene,toluene,1,1,1‐Trichloroethane,o‐xylene,xylenes,arsenic,antimony,beryllium,cadmium,chloride,chromium,chromiumVI,cobalt,fluoride,manganese,mercury,nickel,phosphorus,selenium.
Page 2 of 42Trinity Consultants
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Attachment NTabler Station
TableN‐1.SurfactantMaking‐OutdoorTankEmissions
Throughput1 VaporPressure1 MolecularWeight1 BulkLiquidTemperature1,2 LiquidDensity1 TankCapacity1
EUID (gal/yr) (psia) (lb/lb‐mol) (°F) (lb/gal) (gal) (lb/hr) (tpy) HAPName (lb/hr) (tpy) (lb/hr) (tpy)3 20,327,735 3.50E‐03 197 90.5 6.84 120,762 1.3E‐02 5.5E‐02 ‐‐ ‐‐ ‐‐ ‐‐ ‐‐4 8,805,475 3.42E‐03 197 89.6 7.18 48,345 5.1E‐03 2.2E‐02 EthyleneOxide 5.1E‐03 2.2E‐02 ‐‐ ‐‐5 9,481,192 3.92E‐03 197 95 7.68 40,109 5.5E‐03 2.4E‐02 EthyleneOxide 5.5E‐03 2.4E‐02 ‐‐ ‐‐6 1,917,922 8.62E‐01 46 Ambient 6.58 40,109 2.0E‐01 8.6E‐01 ‐‐ ‐‐ ‐‐ ‐‐ ‐‐7 7,823,046 1.50E‐03 323 99.5 8.69 15,125 2.2E‐03 9.5E‐03 1,4Dioxane 4.6E‐04 2.0E‐03 ‐‐ ‐‐8 7,823,046 1.50E‐03 323 95 8.69 15,125 2.2E‐03 9.6E‐03 1,4Dioxane 4.6E‐04 2.0E‐03 ‐‐ ‐‐9 6,841,173 1.50E‐03 323 95 8.69 15,125 2.0E‐03 8.7E‐03 ‐‐ ‐‐ ‐‐ ‐‐ ‐‐10 39,115,231 1.32E‐03 323 99.5 8.35 72,475 9.4E‐03 4.1E‐02 1,4Dioxane 2.3E‐03 1.0E‐02 ‐‐ ‐‐11 39,115,231 1.32E‐03 323 99.5 8.35 72,475 9.4E‐03 4.1E‐02 1,4Dioxane 2.3E‐03 1.0E‐02 ‐‐ ‐‐12 39,115,231 1.24E‐03 323 95 8.35 72,475 9.0E‐03 3.9E‐02 1,4Dioxane 2.3E‐03 1.0E‐02 ‐‐ ‐‐13 39,115,231 1.24E‐03 323 95 8.35 72,475 9.0E‐03 3.9E‐02 1,4Dioxane 2.3E‐03 1.0E‐02 ‐‐ ‐‐14 34,205,863 1.24E‐03 323 95 8.35 72,475 8.1E‐03 3.6E‐02 ‐‐ ‐‐ ‐‐ ‐‐ ‐‐15 34,205,863 1.24E‐03 323 95 8.35 72,475 8.1E‐03 3.6E‐02 ‐‐ ‐‐ ‐‐ ‐‐ ‐‐16 115,491 1.50E‐03 323 95 8.69 26,083 1.4E‐04 6.3E‐04 ‐‐ ‐‐ ‐‐ ‐‐ ‐‐17 2,000,000 1.69E‐03 98 77 15.36 15,125 ‐‐ -- -- -- -- 3.5E‐04 1.5E‐0318 150,000 1.69E‐03 98 77 15.36 15,125 6.6E‐05 2.9E‐04 ‐‐ ‐‐ ‐‐ ‐‐ ‐‐
2.8E‐01 1.2 ‐‐ 2.1E‐02 9.1E‐02 3.5E‐04 1.5E‐031.ChemicaldataandtankparametersfromProcterandGamble.
3.EmissionscalculatedperAP‐42,Section7.1(OrganicLiquidStorageTanks )andTrinitycalculationsspreadsheets.Specifically,equationscontainedinSection7.1.3.1( TotalLossesfromFixedRoofTanks )areutilized.
4.TraceamountsofHAPbyproductinsurfactant.
VOCPotentialtoEmit3
Total
H2SO4 Potential to Emit3
2.Alltankswillbetemperaturecontrolled(heatedandinsulated)exceptfortheambienttank.Unheatedtankemissionsforcoldmonths(Dec‐Feb)conservativelyassumedtobeequaltomaxwarmmonthemissions.
HAPPotentialtoEmit4
Page 3 of 42Trinity Consultants
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Attachment NTabler Station
TableN‐2.SurfactantMaking‐TruckLoadingEmissions
AmountLoaded
FrequencyLoaded
VaporPressure
MolecularWeight Temp. VOC1 H2SO4
EUID Description (gal/truck) (trucks/yr) (psia) (lb/lb‐mol) R (wt%) wt% VOC H2SO4 VOC H2SO4 VOC H2SO4
PAMTruckLoadout 11,600 13 1.69E‐03 98 528 0.6 100% 30% 2.35E‐03 7.06E‐04 4.0E‐05 1.2E‐05 1.8E‐04 5.3E‐05SurfactantFinalProductTruckLoadout 11,600 1,293 1.50E‐03 323 528 0.6 100% 0% 6.86E‐03 ‐‐ 1.2E‐02 ‐‐ 5.1E‐02 ‐‐
SulfuricAcidTruckLoadout 11,600 172 1.69E‐03 98 528 0.6 0% 100% ‐‐ 2.35E‐03 ‐‐ 5.4E‐04 ‐‐ 2.4E‐03
Total 5.2E‐02 2.4E‐03
1.ConservativelyassumedthatVOCcontentofPAMandsurfactantfinishedproductis100%.
2.LoadinglossemissionfactorscalculatedperAP‐42,Chapter5.2(TransportationandMarketingofPetroleumLiquids ),Equation1.Assumessubmergedfilling.
EmissionFactor(lb/10³gal)2
AnnualEmissions(tpy)
HourlyEmissions(lb/hr)Saturation
Factor
19
Page 4 of 42Trinity Consultants
141801.0078
Attachment NTabler Station
TableN‐3.SurfactantMaking‐ScrubberStack
EmissionsUnit Operation1
EstimatedHoursofOperationfor
System Flowrate2
PollutantConcentration
(ppm)2
PollutantConcentration(mg/m³)
(scfm) NOX NOX NOx CO SO2 VOC PM10/PM2.53 H2SO4 NOx CO SO2 VOC PM10/PM2.5
3 H2SO4
Normal 8,760 5 10.13 5.3E‐01 ‐‐ 1.3E‐01 4.51E‐01 2.1 1.7 2.3 ‐‐ 5.6E‐01 2.0 9.4 7.4
ChangeOver 365 ‐‐ ‐‐ ‐‐ ‐‐ ‐‐ 9.02E‐01 2.59 1.69 ‐‐ ‐‐ ‐‐ 1.65E‐01 4.73E‐01 3.08E‐01
SulfuricAcidProduction 8,760 ‐‐ ‐‐ ‐‐ ‐‐ ‐‐ ‐‐ 8.5E‐01 8.5E‐01 ‐‐ ‐‐ ‐‐ ‐‐ 3.7 3.7
Start‐Up 288 ‐‐ ‐‐ ‐‐ ‐‐ 1.8 ‐‐ 1.7 1.7 ‐‐ ‐‐ 2.60E‐01 ‐‐ 2.43E‐01 2.43E‐01
Normal 8,760 5 10.13 5.3E‐01 ‐‐ 1.3E‐01 4.5E‐01 2.1 1.7 2.3 ‐‐ 5.6E‐01 2.0 9.4 7.4
ChangeOver 156 ‐‐ ‐‐ ‐‐ ‐‐ ‐‐ 9.0E‐01 2.6 1.7 ‐‐ ‐‐ ‐‐ 7.0E‐02 2.0E‐01 1.3E‐01
SulfuricAcidProduction 0 ‐‐ ‐‐ ‐‐ ‐‐ ‐‐ ‐‐ 8.5E‐01 8.5E‐01 ‐‐ ‐‐ ‐‐ ‐‐ ‐‐ ‐‐
Start‐Up 288 ‐‐ ‐‐ ‐‐ ‐‐ 1.8 ‐‐ 1.7 1.7 ‐‐ ‐‐ 2.6E‐01 ‐‐ 2.4E‐01 2.4E‐01
Total 4.7 0.2 1.6 4.2 23.6 19.4
EmissionsUnit Operation1
PollutantConcentration
(ppm)2
PollutantConcentration(mg/m³)
NOX NOX NOx CO SO2 VOC PM10/PM2.53 H2SO4
Normal 5 10.13 5.3E‐01 ‐‐ 1.3E‐01 4.5E‐01 2.1 1.7
ChangeOver ‐‐ ‐‐ 5.3E‐01 ‐‐ ‐‐ 1.4 4.7 3.4
Start‐Up ‐‐ ‐‐ 5.3E‐01 ‐‐ 1.9 ‐‐ 3.4 3.4
Total4 1.1 0.1 2.1 1.80 6.9 5.1
1.Assumesprocessisrunningnormally8,760hoursperyear.ChangeOver/Start‐Up/SulfuricAcidProductionisaddedasadditionalemissionsbeyondthebaseline.
2.Pervendor‐providedspecificationsandemissionsdata.
3.ConservativelyassumesPM10=PM2.5.
4.Maximumhourlyemissionsarecalculatedasthemaximumofthestart‐upandchangeoveremissionsaddedtothenormalemissionsperstack.
AnnualEmissions(tpy)
1Cor2CMaximumHour
14,000
14,0001C
2C
Worst‐CaseHourlyEmissionsPerStack(lb/hr)
NormalHourlyEmissions(lb/hr)
Page 5 of 42Trinity Consultants
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Attachment NTabler Station
TableN‐4.ScrubberPreheaters‐Start‐upOperations 1
NumberofHeaters HeaterRatedCapacityAnnualOperating
HoursNaturalGasHeating
Value(HHV) EmissionFactor(MMBtu/hr) (hr/yr) (Btu/scf) Pollutant (lb/MMscf) Reference (lb/hr) (tpy)
NOx 50 2 7.8E‐01 2.8E‐02CO 84 2 1.3E+00 4.7E‐02PM 7.60 2 1.2E‐01 4.3E‐03PM10 7.60 2 1.2E‐01 4.3E‐03PM2.5 7.60 2 1.2E‐01 4.3E‐03SO2 0.60 2 9.4E‐03 3.4E‐04VOC 5.50 2 8.6E‐02 3.1E‐03H2SO4 6.50E‐03 3 1.0E‐04 3.7E‐06Lead 5.00E‐04 2 7.8E‐06 2.8E‐07
2‐Methylnaphthalene 2.40E‐05 4 3.8E‐07 1.4E‐083‐Methylchloranthrene 1.80E‐06 4 2.8E‐08 1.0E‐09
7,12‐Dimethylbenz(a)anthracene 1.60E‐05 4 2.5E‐07 9.0E‐09
Acenaphthene 1.80E‐06 4 2.8E‐08 1.0E‐09Acenaphthylene 1.80E‐06 4 2.8E‐08 1.0E‐09Anthracene 2.40E‐06 4 3.8E‐08 1.4E‐09
Benz(a)anthracene 1.80E‐06 4 2.8E‐08 1.0E‐09Benzene 2.10E‐03 4 3.3E‐05 1.2E‐06
Benzo(a)pyrene 1.20E‐06 4 1.9E‐08 6.8E‐10Benzo(b)fluoranthene 1.80E‐06 4 2.8E‐08 1.0E‐09Benzo(g,h,i)perylene 1.20E‐06 4 1.9E‐08 6.8E‐10Benzo(k)fluoranthene 1.80E‐06 4 2.8E‐08 1.0E‐09
Chrysene 1.80E‐06 4 2.8E‐08 1.0E‐09Dibenzo(a,h)anthracene 1.20E‐06 4 1.9E‐08 6.8E‐10
Dichlorobenzene 1.20E‐03 4 1.9E‐05 6.8E‐07Fluoranthene 3.00E‐06 4 4.7E‐08 1.7E‐09Fluorene 2.80E‐06 4 4.4E‐08 1.6E‐09
Formaldehyde 7.50E‐02 4 1.2E‐03 4.2E‐05Hexane 1.80E+00 4 2.8E‐02 1.0E‐03
Indeno(1,2,3‐cd)pyrene 1.80E‐06 4 2.8E‐08 1.0E‐09Naphthalene 6.10E‐04 4 9.6E‐06 3.4E‐07Phenanathrene 1.70E‐05 4 2.7E‐07 9.6E‐09
Pyrene 5.00E‐06 4 7.8E‐08 2.8E‐09Toluene 3.40E‐03 4 5.3E‐05 1.9E‐06Arsenic 2.00E‐04 4 3.1E‐06 1.1E‐07Beryllium 1.20E‐05 4 1.9E‐07 6.8E‐09Cadmium 1.10E‐03 4 1.7E‐05 6.2E‐07Chromium 1.40E‐03 4 2.2E‐05 7.9E‐07Cobalt 8.40E‐05 4 1.3E‐06 4.7E‐08Lead 5.00E‐04 4 7.8E‐06 2.8E‐07
Manganese 3.80E‐04 4 6.0E‐06 2.1E‐07Mercury 2.60E‐04 4 4.1E‐06 1.5E‐07Nickel 2.10E‐03 4 3.3E‐05 1.2E‐06
Selenium 2.40E‐05 4 3.8E‐07 1.4E‐082.8E-02 1.0E-033.0E-02 1.1E-03
4.NaturalgasemissionfactorsfromAP‐42,Tables1.4‐3and1.4‐4.
Emissions
4 72 1,020
MaxHAPTotalHAPs
4
1.Duringstartup,combustionemissionsfromthecatalystbedareexhaustedthroughtheSO2scrubber.
2.NaturalgasemissionfactorsfromAP‐42Section1.4.PMassumedtoequalPM10.
3.Naturalgasfactorcalculatedassuming1%ofsulfurbecomesH2SO4.
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TableN‐5.LiquidSoapAandBMaking‐OutdoorTankEmissions
EUID DescriptionThroughput1
VaporPressure
MolecularWeight
LiquidDensity
BulkLiquidTemperature2
TankCapacity1
(gal/yr) (psia) (lb/lb‐mol) (lb/gal) (°F) (gal) (lb/hr) (tpy) HAPName (lb/hr) (tpy)20 RawMaterial 13,431,682 1.32E‐03 323 8.35 113 39,626 3.6E‐03 1.6E‐02 1,4Dioxane 7.9E‐04 3.5E‐0321 RawMaterial 24,833,180 1.24E‐03 323 8.35 113 39,626 5.3E‐03 2.3E‐02 1,4Dioxane 1.5E‐03 6.4E‐0322 RawMaterial 18,189,304 1.24E‐03 323 8.35 113 39,626 4.2E‐03 1.8E‐02 ‐‐ ‐‐ ‐‐23 RawMaterial 291,058 1.24E‐03 323 8.35 113 7,925 2.8E‐04 1.2E‐03 EthyleneOxide 2.8E‐04 1.2E‐0324 RawMaterial 229,500 2.03E‐01 36 9.16 113 7,925 ‐‐ ‐‐ HydrogenChloride 4.2E‐03 1.8E‐0225 RawMaterial 46,050,900 9.28E‐17 343 0.88 113 39,626 7.0E‐16 3.1E‐15 ‐‐ ‐‐ ‐‐26 RawMaterial 685,694 n/a 503 7.51 113 15,850 n/a 0.0E+00 ‐‐ ‐‐ ‐‐27 RawMaterial 2,317,226 1.60E‐03 388 8.97 113 39,626 2.4E‐03 1.0E‐02 ‐‐ ‐‐ ‐‐28 RawMaterial 2,012,364 1.93E‐04 270 6.78 113 26,417 1.5E‐04 6.4E‐04 ‐‐ ‐‐ ‐‐29 RawMaterial 1,039,693 1.16E‐07 242 6.77 113 15,850 4.4E‐08 1.9E‐07 ‐‐ ‐‐ ‐‐30 RawMaterial 1,646,085 7.25E‐05 503 8.35 113 26,417 9.6E‐05 4.2E‐04 ‐‐ ‐‐ ‐‐31 RawMaterial 1,691,510 3.30E‐02 503 8.35 113 15,850 3.0E‐02 1.3E‐01 ‐‐ ‐‐ ‐‐32 RawMaterial 240,216 8.13E‐01 368 7.93 113 15,850 n/a 7.8E‐01 ‐‐ ‐‐ ‐‐33 RawMaterial 282,057 4.83E‐05 92 10.52 77 7,925 5.6E‐07 1.4E‐05 ‐‐ ‐‐ ‐‐34 RawMaterial 146,204 5.00E‐01 200 8.71 Ambient 7,925 7.2E‐02 3.2E‐01 SeeNote4 3.6E‐04 1.6E‐0335 RawMaterial 47,372 5.00E‐01 200 8.71 Ambient 7,925 4.5E‐02 2.0E‐01 SeeNote4 2.3E‐04 9.9E‐0436 RawMaterial 38,244 5.00E‐01 200 8.71 Ambient 7,925 4.3E‐02 1.9E‐01 SeeNote4 2.1E‐04 9.3E‐0437 RawMaterial 7,552 5.00E‐01 200 8.71 Ambient 7,925 3.4E‐02 1.5E‐01 SeeNote4 1.7E‐04 7.4E‐0450 RawMaterial 696,309 1.24E‐03 323 8.35 77 7,925 4.8E‐04 2.1E‐03 ‐‐ ‐‐ ‐‐56 RawMaterial 287,453 1.59E‐03 76 9.09 77 7,275 9.2E‐05 4.0E‐04 ‐‐ ‐‐ ‐‐53 RawMaterial 112,722 1.24E‐03 323 8.35 77 7,925 1.2E‐04 5.26E‐04 ‐‐ ‐‐ ‐‐
2.4E‐01 1.8 ‐‐ 7.7E‐03 3.4E‐02
2.EmissionscalculatedperAP‐42,Section7.1(OrganicLiquidStorageTanks )andTrinitycalculationsspreadsheets.Specifically,equationscontainedinSection7.1.3.1(TotalLossesfromFixedRoofTanks )areutilized.
3.HAPEmissionsfromperfumesassumedtobe0.5%ofVOCemissions.TraceamountofbyproductHAPinsurfactant.
4.Baseduponassessmentofrawmaterialcomposition,HAPspeciationdeterminedtobe99%glycoletherand1%acetophenone.
HAPPotentialtoEmit3VOCPotentialtoEmit2
Total1.TankcapacitiesandthroughputsperProcterandGambledesigndatasheets.
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TableN‐6.LiquidSoapAandBMaking‐IndoorTankEmissions
EUID DescriptionThroughput1
VaporPressure2
MolecularWeight2
LiquidDensity2
BulkLiquidTemperature1
TankCapacity1
(gal/yr) (psia) (lb/lb‐mol) (lb/gal) (°F) (gal) (lb/hr) (tpy) (lb/hr) (tpy)38 RawMaterial 37,808 8.13E‐01 503 8.50 77 396 2.5E‐02 1.1E‐01 ‐‐ ‐‐40 RawMaterial 16,874 5.61E‐02 292 12.02 77 396 7.3E‐04 3.2E‐03 ‐‐ ‐‐41 RawMaterial 12,883 2.90E‐10 205 10.01 77 396 2.0E‐12 8.9E‐12 ‐‐ ‐‐42 RawMaterial 8,007 8.13E‐01 233 8.96 77 396 4.0E‐03 1.8E‐02 ‐‐ ‐‐43 RawMaterial 147,994 8.13E‐01 503 7.93 77 396 4.5E‐02 2.0E‐01 ‐‐ ‐‐44 RawMaterial 11,983 8.13E‐01 503 8.68 77 396 1.3E‐02 5.7E‐02 ‐‐ ‐‐45 RawMaterial 121,569 1.82E‐03 108 8.71 77 396 1.9E‐05 8.4E‐05 ‐‐ ‐‐46 RawMaterial 14,581 4.50E‐01 503 8.31 77 396 8.7E‐03 3.8E‐02 ‐‐ ‐‐47 RawMaterial 8,418 8.13E‐01 503 8.35 77 396 9.1E‐03 4.0E‐02 ‐‐ ‐‐51 RawMaterial n/a n/a n/a n/a 77 396 n/a n/a ‐‐ ‐‐52 RawMaterial 990 1.24E‐03 323 8.35 77 396 1.1E‐06 4.6E‐06 ‐‐ ‐‐54 RawMaterial 267,217 1.24E‐03 323 8.35 77 660 6.5E‐05 2.8E‐04 ‐‐ ‐‐55 RawMaterial 75 8.13E‐01 503 8.50 77 396 8.1E‐05 3.5E‐04 ‐‐ ‐‐57 RawMaterial 24,591 1.59E‐03 76 9.09 77 1,057 6.6E‐06 2.9E‐05 ‐‐ ‐‐59 RawMaterial 2,260 1.59E‐03 76 9.09 77 396 7.2E‐07 3.2E‐06 ‐‐ ‐‐60 RawMaterial 1,953 5.80E‐04 138 8.41 77 132 4.1E‐07 1.8E‐06 4.1E‐07 1.8E‐0661 RawMaterial 175,632 8.13E‐01 503 8.31 77 396 5.0E‐02 2.2E‐01 ‐‐ ‐‐63 RawMaterial 38,430 3.40E‐01 503 7.59 77 396 1.0E‐02 4.5E‐02 ‐‐ ‐‐64 RawMaterial 15,482 0.12 200 8.71 74 396 9.9E‐04 4.3E‐03 4.9E‐06 2.2E‐0565 RawMaterial 14,619 0.12 200 8.71 74 396 9.3E‐04 4.1E‐03 4.7E‐06 2.0E‐0566 RawMaterial 24,900 0.12 200 8.71 74 396 1.3E‐03 5.8E‐03 6.6E‐06 2.9E‐0567 RawMaterial 48,605 0.12 200 8.71 74 396 1.6E‐03 6.9E‐03 7.9E‐06 3.4E‐0568 RawMaterial 26,366 0.12 200 8.71 74 396 1.3E‐03 5.8E‐03 6.7E‐06 2.9E‐0569 RawMaterial 13,652 0.12 200 8.71 74 396 8.7E‐04 3.8E‐03 4.4E‐06 1.9E‐0570 RawMaterial 6,427 0.12 200 8.71 74 396 4.1E‐04 1.8E‐03 2.1E‐06 9.0E‐0671 RawMaterial 12,577 0.12 200 8.71 74 396 8.0E‐04 3.5E‐03 4.0E‐06 1.8E‐0572 RawMaterial 31,508 0.12 200 8.71 74 396 1.4E‐03 6.1E‐03 6.9E‐06 3.0E‐0573 RawMaterial 15,126 0.12 200 8.71 74 396 9.7E‐04 4.2E‐03 4.8E‐06 2.1E‐0574 RawMaterial 64,637 0.12 200 8.71 74 396 1.7E‐03 7.6E‐03 8.7E‐06 3.8E‐0575 RawMaterial 18,314 0.12 200 8.71 74 396 1.2E‐03 5.1E‐03 5.9E‐06 2.6E‐0576 RawMaterial 29,347 0.12 200 8.71 74 396 1.4E‐03 6.0E‐03 6.8E‐06 3.0E‐0577 RawMaterial 43,353 0.12 200 8.71 74 396 1.5E‐03 6.6E‐03 7.6E‐06 3.3E‐05
HAPPotentialtoEmit4VOCPotentialtoEmit2,3
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TableN‐6.LiquidSoapAandBMaking‐IndoorTankEmissions
EUID DescriptionThroughput1
VaporPressure2
MolecularWeight2
LiquidDensity2
BulkLiquidTemperature1
TankCapacity1
(gal/yr) (psia) (lb/lb‐mol) (lb/gal) (°F) (gal) (lb/hr) (tpy) (lb/hr) (tpy)HAPPotentialtoEmit4VOCPotentialtoEmit2,3
87 FinishedProduct 3,799,073 0.0011 200 8.71 90 1,585 4.0E‐04 1.7E‐03 ‐‐ ‐‐88 FinishedProduct 3,799,073 0.0011 200 8.71 90 1,585 3.4E‐04 1.5E‐03 ‐‐ ‐‐89 FinishedProduct 3,799,073 0.0011 200 8.71 90 1,585 3.4E‐04 1.5E‐03 ‐‐ ‐‐90 FinishedProduct 3,799,073 0.0011 200 8.71 90 1,585 3.4E‐04 1.5E‐03 ‐‐ ‐‐91 FinishedProduct 3,799,073 0.0011 200 8.71 90 1,585 3.4E‐04 1.5E‐03 ‐‐ ‐‐92 FinishedProduct 3,799,073 0.0011 200 8.71 90 1,585 3.4E‐04 1.5E‐03 ‐‐ ‐‐93 FinishedProduct 3,799,073 0.0011 200 8.71 90 1,585 3.4E‐04 1.5E‐03 ‐‐ ‐‐94 FinishedProduct 3,799,073 0.0011 200 8.71 90 1,585 3.4E‐04 1.5E‐03 ‐‐ ‐‐94b FinishedProduct 2,048,433 0.0011 200 8.71 90 1,585 2.3E‐04 1.0E‐03 ‐‐ ‐‐94c FinishedProduct 2,048,433 0.0011 200 8.71 90 1,585 2.0E‐04 8.8E‐04 ‐‐ ‐‐94d FinishedProduct 2,048,433 0.0011 200 8.71 90 1,585 2.0E‐04 8.8E‐04 ‐‐ ‐‐94e FinishedProduct 2,048,433 0.0011 200 8.71 90 1,585 2.0E‐04 8.8E‐04 ‐‐ ‐‐95 FinishedProduct 3,973,279 0.0002 200 8.71 90 1,585 6.5E‐05 2.8E‐04 ‐‐ ‐‐96 FinishedProduct 3,973,279 0.0002 200 8.71 90 1,585 5.5E‐05 2.4E‐04 ‐‐ ‐‐97 FinishedProduct 3,973,279 0.0002 200 8.71 90 1,585 5.5E‐05 2.4E‐04 ‐‐ ‐‐98 FinishedProduct 3,973,279 0.0002 200 8.71 90 1,585 5.5E‐05 2.4E‐04 ‐‐ ‐‐99 FinishedProduct 3,973,279 0.0002 200 8.71 90 1,585 5.5E‐05 2.4E‐04 ‐‐ ‐‐100 FinishedProduct 3,973,279 0.0002 200 8.71 90 1,585 5.5E‐05 2.4E‐04 ‐‐ ‐‐101 FinishedProduct 3,973,279 0.0002 200 8.71 90 1,585 5.5E‐05 2.4E‐04 ‐‐ ‐‐102 FinishedProduct 3,973,279 0.0002 200 8.71 90 1,585 5.5E‐05 2.4E‐04 ‐‐ ‐‐103 FinishedProduct 3,973,279 0.0002 200 8.71 90 1,585 5.5E‐05 2.4E‐04 ‐‐ ‐‐104 FinishedProduct 3,973,279 0.0002 200 8.71 90 1,585 5.5E‐05 2.4E‐04 ‐‐ ‐‐105 FinishedProduct 3,973,279 0.0002 200 8.71 90 1,585 5.5E‐05 2.4E‐04 ‐‐ ‐‐106 FinishedProduct 3,973,279 0.0002 200 8.71 90 1,585 5.5E‐05 2.4E‐04 ‐‐ ‐‐107 FinishedProduct 3,973,279 0.0002 200 8.71 90 1,585 5.5E‐05 2.4E‐04 ‐‐ ‐‐108 FinishedProduct 3,973,279 0.0002 200 8.71 90 1,585 5.5E‐05 2.4E‐04 ‐‐ ‐‐109 FinishedProduct 3,973,279 0.0002 200 8.71 90 1,585 5.5E‐05 2.4E‐04 ‐‐ ‐‐110 FinishedProduct 3,973,279 0.0002 200 8.71 90 1,585 5.5E‐05 2.4E‐04 ‐‐ ‐‐111 FinishedProduct 2,048,433 0.0002 200 8.71 90 1,585 3.6E‐05 1.6E‐04 ‐‐ ‐‐112 FinishedProduct 2,048,433 0.0002 200 8.71 90 1,585 3.1E‐05 1.4E‐04 ‐‐ ‐‐113 FinishedProduct 2,048,433 0.0002 200 8.71 90 1,585 3.1E‐05 1.4E‐04 ‐‐ ‐‐114 FinishedProduct 2,048,433 0.0002 200 8.71 90 1,585 3.1E‐05 1.4E‐04 ‐‐ ‐‐115 FinishedProduct 7,786 0.0002 200 8.71 90 1,585 6.9E‐07 3.0E‐06 ‐‐ ‐‐116 FinishedProduct 7,786 0.0002 200 8.71 90 1,585 5.8E‐07 2.5E‐06 ‐‐ ‐‐117 FinishedProduct 7,786 0.0002 200 8.71 90 1,585 5.8E‐07 2.5E‐06 ‐‐ ‐‐118 FinishedProduct 7,786 0.0002 200 8.71 90 1,585 5.8E‐07 2.5E‐06 ‐‐ ‐‐
Total 0.2 0.8 8.2E‐05 3.6E‐04
3.EmissionscalculatedperAP‐42,Section7.1(OrganicLiquidStorageTanks )andTrinitycalculationsspreadsheets.Specifically,equationscontainedinSection7.1.3.1(TotalLossesfromFixedRoofTanks )areutilized.
4.HAPEmissionsfromperfumesassumedtobe0.5%ofVOCemissions.Baseduponassessmentofrawmaterialcomposition,HAPspeciationdeterminedtobe99%glycoletherand1%acetophenone.
1.TankcapacitiesandthroughputsperProcterandGambledesigndatasheets.
2.Finishedproducttanksassumedtocontainafractionalamountofvolatilematerials.
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TableN‐7.SoapMakingBusinessAandB‐FinishedProductPackingandCappingEmissions
Temperature VaporPressure1 Mol.Wt.1 ThroughputEUID Description (°F) (psia) (lb/lb‐mol) (gal/yr) (lb/hr) (tpy)
119SoapMakingBusinessAandBPackingand
CappingLine90 0.0011 200 139,798,617 0.20 2.5E‐04 1.1E‐03
1.Conservativeestimateofproductformulation.
2.KNcalculatedassuminginfinitelymanyturnovers,N,peryear(i.e.,largematerialthroughputandsmallbottlevolume).
3.EmissionscalculatedperAP‐42,Chapter7.1(OrganicLiquidStorageTanks ),Equation1‐29.
Kn2VOCPotentialtoEmit3
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TableN‐8.LiquidSoapAandB‐RotocloneParticulateEmissions
ProcessUnitNumbers
RotocloneNumber1
RotocloneNamePM/PM10/PM2.5
EstimatedControlEfficiency
EmissionFactor1
EmissionFactorUnits
AnnualThroughput2
AnnualThroughput
Units
PM/PM10/PM2.5
Emissions(tons/yr)
120S‐123S 3C PremixRotoclone1 96% 2.00E‐02 gr/dscf 1,182,600,000 scf/yr 1.7124S‐127S 4C LiquidSoapBRotoclone1 96% 2.00E‐02 gr/dscf 2,496,600,000 scf/yr 3.6128S‐131S 5C LiquidSoapBRotoclone2 96% 2.00E‐02 gr/dscf 2,496,600,000 scf/yr 3.6132S‐135S 6C LiquidSoapBRotoclone3 96% 2.00E‐02 gr/dscf 1,655,640,000 scf/yr 2.4
136S‐139S 7C ScaleandLabRotoclone14 96% 2.00E‐02 gr/dscf 525,600,000 scf/yr 0.8
140S‐144S 8C ScaleandLabRotoclone24 96% 2.00E‐02 gr/dscf 525,600,000 scf/yr 0.8146S‐148S 9C LiquidSoapARotoclone1 98% 2.00E‐02 gr/dscf 919,800,000 scf/yr 1.3150S‐152S 10C LiquidSoapARotoclone2 98% 2.00E‐02 gr/dscf 919,800,000 scf/yr 1.3154S‐156S 11C LiquidSoapARotoclone3 98% 2.00E‐02 gr/dscf 919,800,000 scf/yr 1.3158S‐160S 12C LiquidSoapARotoclone4 98% 2.00E‐02 gr/dscf 1,603,080,000 scf/yr 2.3161S‐162S 13C LiquidSoapBRotoclone4 96% 2.00E‐02 gr/dscf 735,840,000 scf/yr 1.1
20.0
2.ConservativeassumptionsbasedonP&GprocessknowledgeforLiquidSoapAandB.ConservativelyassumesPM=PM 10 =PM 2.5
3.Annualthroughputsbasedonmaximumanticipatedproductionvolumes.
Total
1.Controlincludesdustpickuppointsassociatedwithidentifiedprocessunits.Controlonlyoperateswhenpowdersarebeingadded.OthervolatilelossesfrommakingventthroughfugitiveandgeneralprocessventpointsareincludedinoverallVOCemissions.
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TableN‐9.LiquidSoapAandB‐RotocloneandFugitiveVOCEmissions
ProcessUnitNumbers RotocloneNumber1 RotocloneName VOCControlEfficiency EmissionFactor2 EmissionFactorUnits
AnnualThroughput3
(lb/yr)
VOCEmissions(ton/yr)
120S‐123S 3C PremixRotoclone1 0% 1.61E‐02 lb/1000lbs 106,407,288 0.86124S‐127S 4C LiquidSoapBRotoclone1 0% 1.61E‐02 lb/1000lbs 197,299,946 1.59128S‐131S 5C LiquidSoapBRotoclone2 0% 1.61E‐02 lb/1000lbs 238,595,283 1.93132S‐135S 6C LiquidSoapBRotoclone3 0% 1.61E‐02 lb/1000lbs 197,299,946 1.59
136S‐139S 7C ScaleandLabRotoclone14 0% ‐‐ ‐‐ ‐‐ ‐‐
140S‐144S 8C ScaleandLabRotoclone24 0% ‐‐ ‐‐ ‐‐ ‐‐
146S‐148S,150S‐152S,154S‐156S,158S‐160S
9C,10C,11C,12C LiquidSoapAPerfumeLoss 0% 2.60E‐02 lb/1000lbs 179,183,246 2.33
146S‐148S 9C LiquidSoapARotoclone1 0% 1.00E+00 lb/1000lbs150S‐152S 10C LiquidSoapARotoclone2 0% 1.00E+00 lb/1000lbs154S‐156S 11C LiquidSoapARotoclone3 0% 1.00E+00 lb/1000lbs158S‐160S 12C LiquidSoapARotoclone4 0% 1.00E+00 lb/1000lbs161S‐162S 13C LiquidSoapBRotoclone4 0% 1.61E‐02 lb/1000lbs 5,383,423 0.04
33.43
2.EmissionfactorbasedonP&Gprocessknowledge.
3.ThroughputlistedforLiquidSoapAnon‐perfumeVOCisthatwhichcontainsthevolatileprocessingaid.
4.ScaleandLabRotocloneisnotusedformeasuringvolatilematerials.
1.VolatilelossesfrommakingventthroughfugitiveandgeneralprocessventpointsareincludedinoverallVOCemissions.
50,171,309 25.09
TOTAL
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TableN‐10.LiquidSoapA‐RegenerativeThermalOxidizerEmissionsParameter Value Unit
ControlDeviceNumber 14C
EmissionUnitNumbers 145S,149S,153S,157SThroughputofLiquid
SoapA(Total)171,673 tpy
TotalHeatInput 2.4 MMBtu/hrPotentialThroughput 2.35E‐03 MMCF/hr
Pollutant EmissionFactor Units Source
UncontrolledEmissions(lb/hr)
ControlEfficiency(%)
ControlledEmissions(lb/hr)
PTE(tpy)
PM10/PM2.5 7.6 lb/MMCF AP‐42 0.01 0 1.5E‐02 6.5E‐02SO2 6.00E‐01 lb/MMCF AP‐42 1.41E‐03 0 1.4E‐03 6.2E‐03NOX 1.00E‐01 lb/MMBtu Vendor 2.40E‐01 0 2.4E‐01 1.1
VOC‐controlled1,2 5.04 lb/ton MassBalance 213.5 97 6.4 5.4
VOC‐uncontrolled3 5.04 lb/ton MassBalance 213.5 0 213.5 2.6CO 1.33 lb/hr Vendor 1.33 0 1.3 5.8Lead 5.00E‐04 lb/MMCF AP‐42 1.18E‐06 0 1.2E‐06 5.2E‐06
Ammonia 3.2 lb/MMCF FIRE 0.01 0 7.5E‐03 3.30E‐021.BaseduponmaximumthroughputofLiquidSoapAcontainingavolatileprocessingaid.
2.RTOwilloperateonlywhenaHotMixTankforLiquidSoapAwithvolatileprocessingaidisbeingused.
3.Assumes24hours(12‐monthrolling)ofuncontrolledemissionsatmaximumshort‐termsystemcapacity .
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TableN‐11.DryConsumerProductA‐OutdoorTankEmissions
Throughput1 VaporPressureMolecularWeight
BulkLiquidTemperature
LiquidDensity TankCapacity1
EUID (gal/yr) (psia) (lb/lb‐mol) (°F) (lb/gal) (gal) (lb/hr) (tpy) (lb/hr) (tpy)163 7,751,090 7.35E‐09 282 160 7.00 42,879 1.2E‐08 5.1E‐08 ‐‐ ‐‐164 13,608,386 7.35E‐09 282 160 7.97 37,641 1.6E‐08 7.1E‐08 ‐‐ ‐‐165 378,689 0.50 200 77 8.81 6,809 7.0E‐02 3.1E‐01 3.5E‐04 1.5E‐03
7.0E‐02 3.1E‐01 3.5E‐04 1.5E‐03
3.HAPemissionsfromperfumesassumedtobe0.5%ofVOCemissions.Basedonknowledgeofrawmaterials,HAPsare99%glycoletherand1%acetophenone.
2.EmissionscalculatedperAP‐42,Section7.1(OrganicLiquidStorageTanks )andTrinitycalculationsspreadsheets.Specifically,equationscontainedinSection7.1.3.1( TotalLossesfromFixedRoofTanks )areutilized.
VOCPotentialtoEmit2
Total
HAPPotentialtoEmit3
1.TankcapacitiesandthroughputsperProcterandGambledesigndatasheets.ThroughputsaretimeaveragedthroughputsbasedonplannedproductionlinesforothersimilarProcterandGamblefacilitiesandbusinessunits,scaledaccordingtoratioofplannedproductionlinesforthefacility.
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TableN‐12.DryConsumerProductA‐IndoorTankEmissions
Throughput1Vapor
PressureMolecularWeight
BulkLiquidTemperature LiquidDensity TankCapacity1
EUID (gal/yr) (psia) (lb/lb‐mol) (°F) (lb/gal) (gal) (lb/hr) (tpy) (lb/hr) (tpy)166 78,893 0.50 200 77 8.81 396 5.4E‐03 2.4E‐02 2.7E‐05 1.2E‐04167 78,893 0.50 200 77 8.81 396 5.4E‐03 2.4E‐02 2.7E‐05 1.2E‐04168 78,893 0.50 200 77 8.81 396 5.4E‐03 2.4E‐02 2.7E‐05 1.2E‐04169 39,447 0.50 200 77 8.81 181 3.3E‐03 1.4E‐02 1.6E‐05 7.2E‐05170 39,447 0.50 200 77 8.81 181 3.3E‐03 1.4E‐02 1.6E‐05 7.2E‐05171 39,447 0.50 200 77 8.81 181 3.3E‐03 1.4E‐02 1.6E‐05 7.2E‐05172 39,447 0.50 200 77 8.81 181 3.3E‐03 1.4E‐02 1.6E‐05 7.2E‐05173 39,447 0.50 200 77 8.81 181 3.3E‐03 1.4E‐02 1.6E‐05 7.2E‐05174 39,447 0.50 200 77 8.81 181 3.3E‐03 1.4E‐02 1.6E‐05 7.2E‐05175 39,447 0.50 200 77 8.81 181 3.3E‐03 1.4E‐02 1.6E‐05 7.2E‐05176 39,447 0.50 200 77 8.81 181 3.3E‐03 1.4E‐02 1.6E‐05 7.2E‐05177 39,447 0.50 200 77 8.81 181 3.3E‐03 1.4E‐02 1.6E‐05 7.2E‐05178 39,447 0.50 200 77 8.81 181 3.3E‐03 1.4E‐02 1.6E‐05 7.2E‐05179 39,447 0.50 200 77 8.81 181 3.3E‐03 1.4E‐02 1.6E‐05 7.2E‐05180 39,447 0.50 200 77 8.81 181 3.3E‐03 1.4E‐02 1.6E‐05 7.2E‐05181 39,447 0.50 200 77 8.81 181 3.3E‐03 1.4E‐02 1.6E‐05 7.2E‐05182 39,447 0.50 200 77 8.81 181 3.3E‐03 1.4E‐02 1.6E‐05 7.2E‐05183 39,447 0.50 200 77 8.81 181 3.3E‐03 1.4E‐02 1.6E‐05 7.2E‐05184 39,447 0.50 200 77 8.81 181 3.3E‐03 1.4E‐02 1.6E‐05 7.2E‐05185 39,447 0.50 200 77 8.81 181 3.3E‐03 1.4E‐02 1.6E‐05 7.2E‐05186 39,447 0.50 200 77 8.81 181 3.3E‐03 1.4E‐02 1.6E‐05 7.2E‐05187 39,447 0.50 200 77 8.81 181 3.3E‐03 1.4E‐02 1.6E‐05 7.2E‐05188 39,447 0.50 200 77 8.81 181 3.3E‐03 1.4E‐02 1.6E‐05 7.2E‐05
8.1E‐02 3.6E‐01 4.1E‐04 1.8E‐03
2.EmissionscalculatedperAP‐42,Section7.1(OrganicLiquidStorageTanks )andTrinitycalculationsspreadsheets.Specifically,equationscontainedinSection7.1.3.1( TotalLossesfromFixedRoofTanks )areutilized.
3.HAPemissionsfromperfumesassumedtobe0.5%ofVOCemissions.Basedonknowledgeofrawmaterials,HAPsare99%glycoletherand1%acetophenone.
VOCPotentialtoEmit2
Total
HAPPotentialtoEmit3
1.TankcapacitiesandthroughputsperProcterandGambledesigndatasheets.ThroughputsaretimeaveragedthroughputsbasedonplannedproductionlinesforothersimilarProcterandGamblefacilitiesandbusinessunits,scaledaccordingtoratioofplannedproductionlinesforthefacility.
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TableN‐13.DryConsumerProductsA‐ParticulateControlDeviceEmissions
FabricFilterEfficiency1 AirFlowrate2
EUID ControlDeviceID Description ControlType (gr/scf) (scfm) (lb/hr) (tpy)189 15C DryConsumerProductsA‐ClaySilo‐Loading BinVentFilter 8,760 0.02 400 6.9E‐02 3.0E‐01190 16C DryConsumerProductsA‐ClayFRLExhaust Baghouse 8,760 0.02 275 4.7E‐02 2.1E‐01191 17C DryConsumerProductsA‐Feeder/MixerVent Baghouse 8,760 0.02 260 4.5E‐02 2.0E‐01192 18C DryConsumerProductsA‐Line11 Baghouse 8,760 0.010 18,000 1.54E+00 6.8193 19C DryConsumerProductsA‐Line13 Baghouse 8,760 0.010 18,000 1.54E+00 6.8194 20C CVC Baghouse 8,760 0.010 6,500 5.6E‐01 2.4
3.8 16.7
1.ConservativeassumptionsbasedonP&GprocessknowledgeforDryConsumerProductsA
2.PerP&GprocessknowledgeforDryConsumerProductsA
PM/PM10/PM2.5PotentialtoEmitHours/YearUtilized
Total
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TableN‐14.DryConsumerProductsA‐AdditiveEmissionsSubstrateCoated
Area1 TemperatureVaporPressure MolecularWeight
MassTransferCoefficient2
ApplicationFrequency
NumberofLines CoatingMix VOCContent PMCContent
EUID Description (ft²) (°F) (psia) (lb/lb‐mol) (ft/hr) (%) (%) (%) (%) (lb/hr) (tpy)DryConsumerProductsA‐Additive 1,050 50 7.35E‐09 282 39.18 100 2 95 100 n/a 3.1E‐05 1.3E‐04DryConsumerProductsA‐Perfume 1,050 50 1.50E‐02 200 43.93 100 2 5 100 25 2.0 8.7
2.0 8.71.TheproductionlinesaredesignedbasedonthefollowingProcterandGambledesignspecifications.Substratelinespecifications
Substratelength: 2,100 inches2.MassTransferCoefficient(MTC)calculatedusingwater(H2O)asreferencecompound.H2OMTC: 98.03 ft/hrH2OMol.Wt.: 18 lb/lb‐mol
VOCEmissions
195
Total
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TableN‐15.Utilities‐OverallUtilityInventory
Value Units2 50,267 pphsteam1 25,134 pphsteam1 8,918 pphsteam1 331 Mgal/hr1 792 Mgal/hr1 212 Mgal/hr
FirePumpEngine 2 311 hpBackup/StandbyPowerGenerator 3 350 kW
EngineULSDTanks 5 <500 gallonVehicleRefuelingULSDTank 1 5,000 gallon
WarehouseHeaters 6 3.05 MMBtu/hr
WeightedHeatofVaporization1
Value Units (Btu/lb) Value Units2 50,267 pphsteam 1,048.4 85% 62 MMBtu/hr1 25,134 pphsteam 1,048.4 85% 31 MMBtu/hr1 8,918 pphsteam 1,048.4 85% 11 MMBtu/hr
1.Steamparameters:
H2Oheatofvaporization(non‐condensatereturn): 1,178 Btu/lb
H2Oheatofvaporization(condensatereturn): 1,016 Btu/lb
Condensatereturn: 80%
Boilers
DesignSize BoilerEfficiency(HHV)
CalculatedSize
DesignSize
CoolingTowers
EquipmentType Quantity
QuantityEquipmentType
Boilers
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TableN‐16.Utilities‐BoilerNos.1and2‐CriteriaPollutants
Value6225438,7601,000
HourlyEmissions(lb/hr)
AnnualEmissions(tpy)
NOX 60 ppm 2 4.5 19.8 39.5
CO 50 ppm 2 2.3 10.0 20.1
PM 3.80E‐03 lb/MMBtu 2 2.4E‐01 1.0 2.1
PM10 7.50E‐03 lb/MMBtu 2 4.7E‐01 2.0 4.1
PM2.5 7.50E‐03 lb/MMBtu 2 4.7E‐01 2.0 4.1
SO2 6.00E‐04 lb/MMBtu 2 3.7E‐02 1.6E‐01 3.3E‐01
VOC 3.60E‐03 lb/MMBtu 2 2.2E‐01 1.0 2.0
H2SO4 6.50E‐03 lb/MMscf 3 4.0E‐04 1.8E‐03 3.5E‐03
Parameter UnitNewBoilerHeatInput: MMBtu/hrNumberofNewBoilers:AnnualGasUsage: MMscf/yr
EquivalentGasHours: Hoursat100%LoadNaturalGasHeatingValue(HHV): Btu/scf
EmissionsforBoilers1and
2(tpy)
1.Naturalgasfactorsbasedonmanufacturer'sppmspecificationsforunitswithLNBandconvertedtolb/MMBtuusinganFfactorof8,710dscf/MMBtufornaturalgas.
2.Guaranteesfromboilervendor.
3.Naturalgasfactorcalculatedassuming1%ofsulfurbecomesH2SO4.
PollutantNaturalGasEmissionFactor
Units Reference
EmissionsPerBoiler
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TableN‐17.Utilities‐BoilerNos.1and2‐HAPValue Unit62 MMBtu/hr2
8,760 hr/yr1,020 Btu/scf
lb/hr tpy lb/hr tpy
2‐Methylnaphthalene 2.4E‐05 lb/MMscf 1.5E‐06 6.4E‐06 2.9E‐06 1.3E‐053‐Methylchloranthrene 1.8E‐06 lb/MMscf 1.1E‐07 4.8E‐07 2.2E‐07 9.6E‐07
7,12‐Dimethylbenz(a)anthracene 1.6E‐05 lb/MMscf 9.7E‐07 4.3E‐06 1.9E‐06 8.5E‐06Acenaphthene 1.8E‐06 lb/MMscf 1.1E‐07 4.8E‐07 2.2E‐07 9.6E‐07Acenaphthylene 1.8E‐06 lb/MMscf 1.1E‐07 4.8E‐07 2.2E‐07 9.6E‐07Anthracene 2.4E‐06 lb/MMscf 1.5E‐07 6.4E‐07 2.9E‐07 1.3E‐06
Benz(a)anthracene 1.8E‐06 lb/MMscf 1.1E‐07 4.8E‐07 2.2E‐07 9.6E‐07Benzene 2.1E‐03 lb/MMscf 1.3E‐04 5.6E‐04 2.6E‐04 1.1E‐03
Benzo(a)pyrene 1.2E‐06 lb/MMscf 7.3E‐08 3.2E‐07 1.5E‐07 6.4E‐07Benzo(b)fluoranthene 1.8E‐06 lb/MMscf 1.1E‐07 4.8E‐07 2.2E‐07 9.6E‐07Benzo(g,h,i)perylene 1.2E‐06 lb/MMscf 7.3E‐08 3.2E‐07 1.5E‐07 6.4E‐07Benzo(k)fluoranthene 1.8E‐06 lb/MMscf 1.1E‐07 4.8E‐07 2.2E‐07 9.6E‐07
Chrysene 1.8E‐06 lb/MMscf 1.1E‐07 4.8E‐07 2.2E‐07 9.6E‐07Dibenzo(a,h)anthracene 1.2E‐06 lb/MMscf 7.3E‐08 3.2E‐07 1.5E‐07 6.4E‐07
Dichlorobenzene 1.2E‐03 lb/MMscf 7.3E‐05 3.2E‐04 1.5E‐04 6.4E‐04Fluoranthene 3.0E‐06 lb/MMscf 1.8E‐07 8.0E‐07 3.6E‐07 1.6E‐06Fluorene 2.8E‐06 lb/MMscf 1.7E‐07 7.5E‐07 3.4E‐07 1.5E‐06
Formaldehyde 7.5E‐02 lb/MMscf 4.6E‐03 2.0E‐02 9.1E‐03 4.0E‐02Hexane 1.8E+00 lb/MMscf 1.1E‐01 4.8E‐01 2.2E‐01 9.6E‐01
Indeno(1,2,3‐cd)pyrene 1.8E‐06 lb/MMscf 1.1E‐07 4.8E‐07 2.2E‐07 9.6E‐07Naphthalene 6.1E‐04 lb/MMscf 3.7E‐05 1.6E‐04 7.4E‐05 3.2E‐04Phenanathrene 1.7E‐05 lb/MMscf 1.0E‐06 4.5E‐06 2.1E‐06 9.1E‐06
Pyrene 5.0E‐06 lb/MMscf 3.0E‐07 1.3E‐06 6.1E‐07 2.7E‐06Toulene 3.4E‐03 lb/MMscf 2.1E‐04 9.1E‐04 4.1E‐04 1.8E‐03Arsenic 2.0E‐04 lb/MMscf 1.2E‐05 5.3E‐05 2.4E‐05 1.1E‐04Beryllium 1.2E‐05 lb/MMscf 7.3E‐07 3.2E‐06 1.5E‐06 6.4E‐06Cadmium 1.1E‐03 lb/MMscf 6.7E‐05 2.9E‐04 1.3E‐04 5.9E‐04Chromium 1.4E‐03 lb/MMscf 8.5E‐05 3.7E‐04 1.7E‐04 7.5E‐04Cobalt 8.4E‐05 lb/MMscf 5.1E‐06 2.2E‐05 1.0E‐05 4.5E‐05Lead 5.0E‐04 lb/MMscf 3.0E‐05 1.3E‐04 6.1E‐05 2.7E‐04
Manganese 3.8E‐04 lb/MMscf 2.3E‐05 1.0E‐04 4.6E‐05 2.0E‐04Mercury 2.6E‐04 lb/MMscf 1.6E‐05 6.9E‐05 3.2E‐05 1.4E‐04Nickel 2.1E‐03 lb/MMscf 1.3E‐04 5.6E‐04 2.6E‐04 1.1E‐03
Selenium 2.40E‐05 lb/MMscf 1.5E‐06 6.4E‐06 2.9E‐06 1.3E‐05TotalHAP 2.3E‐01 1.0E+00
1.NaturalgasemissionfactorsfromAP‐42,Tables1.4‐3and1.4‐4
Units
EmissionsforBoilers1and2
ParameterNewBoilerHeatInput:NumberofNewBoilers:
HoursofOperationonNaturalGas:NaturalGasHeatingValue(HHV):
PollutantNaturalGas
EmissionFactor1EmissionsPerBoiler
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TableN‐18.Utilities‐BoilerNos.3‐Parameters
Value3112728,7601,000
NOX 60 ppm 2 2.3 9.9 9.9
CO 50 ppm 2 1.1 5.0 5.0
PM 3.80E‐03 lb/MMBtu 2 1.2E‐01 0.5 0.5
PM10 7.50E‐03 lb/MMBtu 2 2.3E‐01 1.0 1.0
PM2.5 7.50E‐03 lb/MMBtu 2 2.3E‐01 1.0 1.0
SO2 6.00E‐04 lb/MMBtu 2 1.9E‐02 8.1E‐02 8.1E‐02
VOC 3.60E‐03 lb/MMBtu 2 1.1E‐01 4.9E‐01 4.9E‐01
H2SO4 6.50E‐03 lb/MMscf 3 2.0E‐04 8.8E‐04 8.8E‐04
1.Naturalgasemissionfactorsbasedonmanufacturer'sppmspecificationsforunitswithLNBandconvertedtolb/MMBtuusinganFfactorof8,710dscf/MMBtufornaturalgas.
3.Naturalgasfactorcalculatedassuming1%ofsulfurbecomesH 2SO4.
2.Guaranteesfromboilervendor.
NaturalGasHourly
Emissions(lb/hr)
NaturalGasAnnual
Emissions(tpy)
Emissionsfor
Boiler3
(tpy)
PollutantNaturalGasEmissionFactor
Units Reference
NaturalGasHeatingValue(HHV): Btu/scfEquivalentGasHours: Hoursat100%LoadAnnualGasUsage: MMscf/yr
Parameter UnitNewBoilerHeatInput: MMBtu/hrNumberofNewBoilers:
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TableN‐19.Utilities‐BoilerNos.3‐ParametersValue Unit31 MMBtu/hr1
8,760 hr/yr1,020 Btu/scf
lb/hr tpy
2‐Methylnaphthalene 2.4E‐05 lb/MMscf 7.3E‐07 3.2E‐063‐Methylchloranthrene 1.8E‐06 lb/MMscf 5.5E‐08 2.4E‐07
7,12‐Dimethylbenz(a)anthracene 1.6E‐05 lb/MMscf 4.9E‐07 2.1E‐06Acenaphthene 1.8E‐06 lb/MMscf 5.5E‐08 2.4E‐07Acenaphthylene 1.8E‐06 lb/MMscf 5.5E‐08 2.4E‐07Anthracene 2.4E‐06 lb/MMscf 7.3E‐08 3.2E‐07
Benz(a)anthracene 1.8E‐06 lb/MMscf 5.5E‐08 2.4E‐07Benzene 2.1E‐03 lb/MMscf 6.4E‐05 2.8E‐04
Benzo(a)pyrene 1.2E‐06 lb/MMscf 3.6E‐08 1.6E‐07Benzo(b)fluoranthene 1.8E‐06 lb/MMscf 5.5E‐08 2.4E‐07Benzo(g,h,i)perylene 1.2E‐06 lb/MMscf 3.6E‐08 1.6E‐07Benzo(k)fluoranthene 1.8E‐06 lb/MMscf 5.5E‐08 2.4E‐07
Chrysene 1.8E‐06 lb/MMscf 5.5E‐08 2.4E‐07Dibenzo(a,h)anthracene 1.2E‐06 lb/MMscf 3.6E‐08 1.6E‐07
Dichlorobenzene 1.2E‐03 lb/MMscf 3.6E‐05 1.6E‐04Fluoranthene 3.0E‐06 lb/MMscf 9.1E‐08 4.0E‐07Fluorene 2.8E‐06 lb/MMscf 8.5E‐08 3.7E‐07
Formaldehyde 7.5E‐02 lb/MMscf 2.3E‐03 1.0E‐02Hexane 1.8E+00 lb/MMscf 5.5E‐02 2.4E‐01
Indeno(1,2,3‐cd)pyrene 1.8E‐06 lb/MMscf 5.5E‐08 2.4E‐07Naphthalene 6.1E‐04 lb/MMscf 1.9E‐05 8.1E‐05Phenanathrene 1.7E‐05 lb/MMscf 5.2E‐07 2.3E‐06
Pyrene 5.0E‐06 lb/MMscf 1.5E‐07 6.7E‐07Toulene 3.4E‐03 lb/MMscf 1.0E‐04 4.5E‐04Arsenic 2.0E‐04 lb/MMscf 6.1E‐06 2.7E‐05Beryllium 1.2E‐05 lb/MMscf 3.6E‐07 1.6E‐06Cadmium 1.1E‐03 lb/MMscf 3.3E‐05 1.5E‐04Chromium 1.4E‐03 lb/MMscf 4.3E‐05 1.9E‐04Cobalt 8.4E‐05 lb/MMscf 2.6E‐06 1.1E‐05Lead 5.0E‐04 lb/MMscf 1.5E‐05 6.7E‐05
Manganese 3.8E‐04 lb/MMscf 1.2E‐05 5.1E‐05Mercury 2.6E‐04 lb/MMscf 7.9E‐06 3.5E‐05Nickel 2.1E‐03 lb/MMscf 6.4E‐05 2.8E‐04
Selenium 2.40E‐05 lb/MMscf 7.3E‐07 3.2E‐06TotalHAP 5.7E‐02 2.5E‐01
Emissions
1.NaturalgasemissionfactorsfromAP‐42,Tables1.4‐3and1.4‐4
PollutantNaturalGas
EmissionFactor1Units
ParameterNewBoilerHeatInput:NumberofNewBoilers:
HoursofOperationonNaturalGas:NaturalGasHeatingValue(HHV):
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TableN‐20.Utilities‐CoolingTowers‐Emissions
Parameter Unit1 Unit2 Unit3 EmissionsTotal
Location1 Surfactants CentralUtilities LiquidSoapAandB ‐‐
FlowRate(gpm)1 5,517 13,200 3,533 ‐‐
FlowRate(Mgal/hr) 331 792 212 ‐‐
FlowRate(Mgal/yr) 2,899,560 6,937,920 1,857,120 ‐‐
OperatingHours(hr/yr) 8,760 8,760 8,760 ‐‐
DensityofWater(lb/gal) 8.35 8.35 8.35 ‐‐
TotalDissolvedSolids,TDS(ppm) 1,600 1,600 1,600 ‐‐
Drift(%)2 5.00E‐03 5.00E‐03 5.00E‐03 ‐‐
Drift(gpm) 0.28 0.66 0.18 ‐‐
PM/PM10/PM2.5(lb/gal)3 6.7E‐07 6.7E‐07 6.7E‐07 ‐‐
PM/PM10/PM2.5(lb/hr) 2.2E‐01 5.3E‐01 1.4E‐01 0.9
PM/PM10/PM2.5(tpy) 1.0 2.3 0.6 3.9
3.PM10areconservativelyoverestimatedby(TDS,ppm)x(TotalDriftRate,lb/gal)/106,basedonAP‐42Section13.4‐3.
1.Clientspecification.
2.DriftPercentageforInducedDraftCoolerspecifiedinemailfromBrianMensinger(TrinityConsultants)toAllisonCole(TrinityConsultants)onJuly22,2015.
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TableN‐21.Utilities‐Engines‐InventorySummaryEngineModel Type Number Size UnitCaterpillarC15 Backup/StandbyPowerGenerator 3 350 kW
ClarkeJW6H‐UFADF0 FirePump 2 311 hp
PollutantPotentialEmissionsperEngine,
CaterpillarC15(tpy)
PotentialEmissionsperEngine,Clarke
(tpy)
Emissions(tpy)
CO 1.4E‐01 1.4E‐01 6.9E‐01NOX 8.7E‐01 4.5E‐01 3.5VOC 1.1E‐02 1.7E‐02 6.7E‐02SO2 3.6E‐04 2.4E‐04 1.6E‐03PM 1.2E‐02 1.7E‐02 7.0E‐02PM10 1.2E‐02 1.7E‐02 6.9E‐02PM2.5 1.2E‐02 1.7E‐02 6.9E‐02
PollutantPotentialEmissionsperEngine,
CaterpillarC15(tpy)
PotentialEmissionsperEngine,Clarke
(tpy)
Emissions(tpy)
Benzene 7.7E‐04 5.1E‐04 3.3E‐03Toluene 3.4E‐04 2.2E‐04 1.5E‐03Xylenes 2.4E‐04 1.6E‐04 1.0E‐03Propylene 2.1E‐03 1.4E‐03 9.2E‐03
Formaldehyde 9.8E‐04 6.4E‐04 4.2E‐03Acetaldehyde 6.4E‐04 4.2E‐04 2.7E‐03Acrolein 7.7E‐05 5.0E‐05 3.3E‐04
PolycyclicAromaticHydrocarbons(PAH) 1.4E‐04 9.1E‐05 6.0E‐04MaxHAP 2.1E‐03 1.4E‐03 9.2E‐03TotalHAPs 5.3E‐03 3.5E‐03 2.3E‐02
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TableN‐22.Utilities‐Engines‐Caterpillar350kWSourceDesignation Engine GeneratorDateManufactured TBD TBD
Manufacturer1 Caterpillar Caterpillar
ModelNo.2 C15 C15
StrokeCycle2 4‐Stroke ‐‐
FuelUsed2 Diesel ‐‐
FuelSulfurContent(%)3 0.0015 ‐‐
RatedCapacity(eKW)2 350.00 ‐‐
CalculatedHorsepower(bhp)4 473.69 ‐‐
GeneratingCapacity(kW)1 ‐‐ 350.00
MaximumFuelConsumptionat100%Load(gal/hr)2 28.60 ‐‐
HeatInput(MMBtu/hr)5 3.32 ‐‐
OperationalDetail ValuePotentialAnnualHoursofOperation(hr/yr): 500.00
PotentialFuelConsumption(Mgal/yr): 14.30
Pollutant EmissionFactors Units NotesCO 5.30E‐01 g/hp‐hr 2NOX 3.34 g/hp‐hr 2HC 4.18E‐02 g/hp‐hr 2,6SO2 3.08E‐06 lb/hp‐hr 7PM 4.60E‐02 g/hp‐hr 2,8PM10 4.60E‐02 g/hp‐hr 2,8PM2.5 4.60E‐02 g/hp‐hr 2,8
TableN‐24.Utilities‐Engines‐Caterpillar350kW
PotentialEmissions PotentialEmissions
(lb/hr)11 (tpy)CO 5.5E‐01 1.4E‐01NOx 3.5E+00 8.7E‐01VOC 4.4E‐02 1.1E‐02SO2 1.5E‐03 3.6E‐04PM 4.8E‐02 1.2E‐02PM10 4.6E‐02 1.2E‐02PM2.5 4.6E‐02 1.2E‐02
EmissionFactor PotentialEmissions PotentialEmissions
(lb/MMBtu)10 (lb/hr)9 (tpy)Benzene 9.33E‐04 3.1E‐03 7.7E‐04Toluene 4.09E‐04 1.4E‐03 3.4E‐04Xylenes 2.85E‐04 9.5E‐04 2.4E‐04Propylene 2.58E‐03 8.6E‐03 2.1E‐03
Formaldehyde 1.18E‐03 3.9E‐03 9.8E‐04Acetaldehyde 7.67E‐04 2.5E‐03 6.4E‐04Acrolein 9.25E‐05 3.1E‐04 7.7E‐05
PolycyclicAromaticHydrocarbons(PAH) 1.68E‐04 5.6E‐04 1.4E‐048.6E‐03 2.1E‐032.1E‐02 5.3E‐03
Pollutant
Pollutant
MaxHAPTotalHAPs
1.Clientspecification.
2.Valuescomefromtheunit'sspecsheet"CaterpillarC15ATAACDieselEngine."Foundathttp://s7d2.scene7.com/is/content/caterpillar/C10059394.
3.Per40CFR80SubpartI,maximumsulfurcontentofULSDis15ppm(i.e.0.0015%).
4.Dieselgeneratorhorsepower(BHP)backcalculatedfromelectricgeneratorratedoutput(ekW).Aninefficiencyof1%wasincludedtoaccountforlossesfromshaftworktoelectricity.
5.ToconvertfrombhptoMMBtu/hr,anaveragebrake‐specificfuelconsumptionof7,000Btu/hp‐hrwasusedperAP‐42P‐42Section3.3,Table3.3‐1"EmissionFactorsforUncontrolledGasolineandDieselIndustrialEngines,"SupplementB,October1996.
6.Allhydrocarbon(HC)emissionsareconservativelyassumedtobeVOC.
7.SO2emissionfactorfromAP‐42Section3.3,Table3.3‐1"EmissionFactorsforUncontrolledGasolineandDieselIndustrialEngines,"SupplementB,October1996.
9.EmissionRate(lb/hr)=RatedCapacity(MMBtu/hrorbhp)×EmissionFactor(lb/MMBtuorlb/bhp‐hr).
10.EmissionfactorsfromAP‐42Section3.3,Table3.3‐2"SpeciatedOrganicCompoundEmissionFactorsforUncontrolledDieselEngines."
8.Allparticulatesareassumedtobe<1microninsize,wherePM,PM 10,andPM2.5 areassumedtobeequivalent,consistentwithAP‐42Section3.3,Table3.3‐1"EmissionFactorsforUncontrolledGasolineandDieselIndustrialEngines,"SupplementB,October1996.
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TableN‐23.Utilities‐Engines‐ClarkeSourceDesignation EngineDateManufactured TBD
Manufacturer1 Clarke
ModelNo.2 JW6H‐UFADF0
StrokeCycle2 4‐Stroke
FuelUsed1 Diesel
FuelSulfurContent(%)3 0.0015
RatedHorsepower(bhp)2 311.00
MaximumFuelConsumptionat100%Load(gal/hr)4 16.13
HeatInput(MMBtu/hr)5 2.18
OperationalDetail ValuePotentialAnnualHoursofOperation(hr/yr): 500.00
PotentialFuelConsumption(Mgal/yr): 8.06
Pollutant EmissionFactors Units NotesCO 8.00E‐01 g/hp‐hr 6
NOX 2.61 g/hp‐hr 6
HC 1.00E‐01 g/hp‐hr 6,7
SO2 3.08E‐06 lb/hp‐hr 8
PM 1.00E‐01 g/hp‐hr 6,9
PM10 1.00E‐01 g/hp‐hr 6,9
PM2.5 1.00E‐01 g/hp‐hr 6,9
TableN‐26.Utilities‐Engines‐ClarkePotentialEmissions PotentialEmissions
(lb/hr)10 (tpy)CO 5.5E‐01 1.4E‐01
NOX 1.8 4.5E‐01
VOC 6.9E‐02 1.7E‐02
SO2 9.6E‐04 2.4E‐04
PM 6.9E‐02 1.7E‐02
PM10 6.9E‐02 1.7E‐02
PM2.5 6.9E‐02 1.7E‐02
EmissionFactor PotentialEmissions PotentialEmissions
(lb/MMBtu)11 (lb/hr)10 (tpy)Benzene 9.33E‐04 2.0E‐03 5.1E‐04Toluene 4.09E‐04 8.9E‐04 2.2E‐04Xylenes 2.85E‐04 6.2E‐04 1.6E‐04Propylene 2.58E‐03 5.6E‐03 1.4E‐03
Formaldehyde 1.18E‐03 2.6E‐03 6.4E‐04Acetaldehyde 7.67E‐04 1.7E‐03 4.2E‐04Acrolein 9.25E‐05 2.0E‐04 5.0E‐05
PolycyclicAromaticHydrocarbons(PAH) 1.68E‐04 3.7E‐04 9.1E‐055.6E‐03 1.4E‐031.4E‐02 3.5E‐03
Pollutant
Pollutant
MaxHAPTotalHAPs
1.Clientspecification.
8.SO2emissionfactorfromAP‐42Section3.3,Table3.3‐1"EmissionFactorsforUncontrolledGasolineandDieselIndustrialEngines,"SupplementB,October1996.
2.Valuescomefromtheunit'sspecsheet"ClarkeJW6H‐UFADJ0FireEngineSpecifications."Foundathttp://www.clarkefire.com/Libraries/PDF/Spec_Sheet_JW6H‐UFAA‐AD_C133422.sflb.ashx
3.Per40CFR80SubpartI,maximumsulfurcontentofULSDis15ppm(i.e.0.0015%).
4.Maximumfuelconsumptioncalculatedastheheatinputfortheengine(MMBtu)dividedbytheenergydensityofdieselfuel(0.135MMBtu/gal).
5.ToconvertfrombhptoMMBtu/hr,anaveragebrake‐specificfuelconsumptionof7,000Btu/hp‐hrwasusedperAP‐42P‐42Section3.3,Table3.3‐1"EmissionFactorsforUncontrolledGasolineandDieselIndustrialEngines,"SupplementB,October1996.
6.NOX,HC,CO,andPMemissionfactorsfromJohnDeere"RatingSpecificEmissionsData."Foundathttp://www.clarkefire.com/Libraries/PDF/Emissions_JW6H‐UFADF0_6090HFC47A_1760rpm_2009.sflb.ashx
7.Toconservativelyover‐estimateemissions,allhydrocarbon(HC)emissionsareassumedtobeVOC.
10.EmissionRate(lb/hr)=RatedCapacity(MMBtu/hrorbhp)×EmissionFactor(lb/MMBtuorlb/bhp‐hr).
11.EmissionfactorsfromAP‐42Section3.3,Table3.3‐2"SpeciatedOrganicCompoundEmissionFactorsforUncontrolledDieselEngines."
9.Allparticulatesareassumedtobe<1microninsize,wherePM,PM 10,andPM2.5areassumedtobeequivalent,consistentwithAP‐42Section3.3,Table3.3‐1"EmissionFactorsforUncontrolledGasolineandDieselIndustrialEngines,"SupplementB,October1996.
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TableN‐24.Utilities‐DieselTank‐Emissions
ThroughputVapor
Pressure1MolecularWeight1
BulkLiquidTemperature LiquidDensity1 TotalCapacity
EUID Description (gal/yr) (psia) (lb/lb‐mol) (°F) (lb/gal) (gal) (lb/hr) (tpy)
208 Diesel(DistillateFuelOilNo.2) 70,000 2.20E‐02 130 Ambient 7.1 5,162 5.2E‐04 2.3E‐035.2E‐04 2.3E‐03
1.ChemicalpropertiesperEPATANKS4.09ddatabasefordistillatefueloilno.2.
VOCEmissions2
Total
2.EmissionscalculatedperAP‐42,Section7.1(OrganicLiquidStorageTanks )andTrinitycalculationsspreadsheets.Specifically,equationscontainedinSection7.1.3.1(TotalLossesfromFixedRoofTanks )areutilized.
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TableN‐25.Utilities‐Heaters
Value Unit
3.05 MMBtu/hr
8,760 hr/yr
1,020 Btu/scf
26.18 MMscf/yr
6
NOX 50.00 lb/MMscf 1 1.49E‐01 6.5E‐01 3.9
CO 84.00 lb/MMscf 1 2.51E‐01 1.1 6.6
PM 7.60 lb/MMscf 1 2.27E‐02 9.9E‐02 6.0E‐01
PM10 7.60 lb/MMscf 1 2.27E‐02 9.9E‐02 6.0E‐01
PM2.5 7.60 lb/MMscf 1 2.27E‐02 9.9E‐02 6.0E‐01
SO2 0.60 lb/MMscf 1 1.79E‐03 7.9E‐03 4.7E‐02
VOC 5.50 lb/MMscf 1 1.64E‐02 7.2E‐02 4.3E‐01
H2SO4 6.50E‐03 lb/MMscf 2 1.94E‐05 8.5E‐05 5.1E‐04
NumberofHeaters:
Parameter
1.NaturalgasemissionfactorsfromAP‐42Section1.4.PMassumedtoequalPM10.
HeaterSize:
OperatingHours:
NaturalGasHeatingValue(HHV):
AnnualGasUsage:
2.Naturalgasfactorcalculatedassuming1%ofsulfurbecomesH2SO4.
Units Reference
HourlyEmissionsperHeater(lb/hr)
AnnualEmissionsperHeater(tpy)
AnnualEmissionsforAllHeaters
(tpy)
PollutantNaturalGas
EmissionFactor
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TableN‐26.Utilities‐HeatersParameter Value UnitHeaterSize: 3.05 MMBtu/hr
NumberofHeaters: 6HoursofOperation: 8,760 hr/yr
NaturalGasHeatingValue(HHV): 1,020 Btu/scf
lb/hr tpy lb/hr tpy
2‐Methylnaphthalene 2.40E‐05 lb/MMscf 7.2E‐08 3.1E‐07 4.3E‐07 1.9E‐063‐Methylchloranthrene 1.80E‐06 lb/MMscf 5.4E‐09 2.4E‐08 3.2E‐08 1.4E‐07
7,12‐Dimethylbenz(a)anthracene 1.60E‐05 lb/MMscf 4.8E‐08 2.1E‐07 2.9E‐07 1.3E‐06Acenaphthene 1.80E‐06 lb/MMscf 5.4E‐09 2.4E‐08 3.2E‐08 1.4E‐07Acenaphthylene 1.80E‐06 lb/MMscf 5.4E‐09 2.4E‐08 3.2E‐08 1.4E‐07Anthracene 2.40E‐06 lb/MMscf 7.2E‐09 3.1E‐08 4.3E‐08 1.9E‐07
Benz(a)anthracene 1.80E‐06 lb/MMscf 5.4E‐09 2.4E‐08 3.2E‐08 1.4E‐07Benzene 2.10E‐03 lb/MMscf 6.3E‐06 2.7E‐05 3.8E‐05 1.6E‐04
Benzo(a)pyrene 1.20E‐06 lb/MMscf 3.6E‐09 1.6E‐08 2.2E‐08 9.4E‐08Benzo(b)fluoranthene 1.80E‐06 lb/MMscf 5.4E‐09 2.4E‐08 3.2E‐08 1.4E‐07Benzo(g,h,i)perylene 1.20E‐06 lb/MMscf 3.6E‐09 1.6E‐08 2.2E‐08 9.4E‐08Benzo(k)fluoranthene 1.80E‐06 lb/MMscf 5.4E‐09 2.4E‐08 3.2E‐08 1.4E‐07
Chrysene 1.80E‐06 lb/MMscf 5.4E‐09 2.4E‐08 3.2E‐08 1.4E‐07Dibenzo(a,h)anthracene 1.20E‐06 lb/MMscf 3.6E‐09 1.6E‐08 2.2E‐08 9.4E‐08
Dichlorobenzene 1.20E‐03 lb/MMscf 3.6E‐06 1.6E‐05 2.2E‐05 9.4E‐05Fluoranthene 3.00E‐06 lb/MMscf 9.0E‐09 3.9E‐08 5.4E‐08 2.4E‐07Fluorene 2.80E‐06 lb/MMscf 8.4E‐09 3.7E‐08 5.0E‐08 2.2E‐07
Formaldehyde 7.50E‐02 lb/MMscf 2.2E‐04 9.8E‐04 1.3E‐03 5.9E‐03Hexane 1.80E+00 lb/MMscf 5.4E‐03 2.4E‐02 3.2E‐02 1.4E‐01
Indeno(1,2,3‐cd)pyrene 1.80E‐06 lb/MMscf 5.4E‐09 2.4E‐08 3.2E‐08 1.4E‐07Naphthalene 6.10E‐04 lb/MMscf 1.8E‐06 8.0E‐06 1.1E‐05 4.8E‐05Phenanathrene 1.70E‐05 lb/MMscf 5.1E‐08 2.2E‐07 3.0E‐07 1.3E‐06
Pyrene 5.00E‐06 lb/MMscf 1.5E‐08 6.5E‐08 9.0E‐08 3.9E‐07Toulene 3.40E‐03 lb/MMscf 1.0E‐05 4.5E‐05 6.1E‐05 2.7E‐04Arsenic 2.00E‐04 lb/MMscf 6.0E‐07 2.6E‐06 3.6E‐06 1.6E‐05Beryllium 1.20E‐05 lb/MMscf 3.6E‐08 1.6E‐07 2.2E‐07 9.4E‐07Cadmium 1.10E‐03 lb/MMscf 3.3E‐06 1.4E‐05 2.0E‐05 8.6E‐05Chromium 1.40E‐03 lb/MMscf 4.2E‐06 1.8E‐05 2.5E‐05 1.1E‐04Cobalt 8.40E‐05 lb/MMscf 2.5E‐07 1.1E‐06 1.5E‐06 6.6E‐06Lead 5.00E‐04 lb/MMscf 1.5E‐06 6.5E‐06 9.0E‐06 3.9E‐05
Manganese 3.80E‐04 lb/MMscf 1.1E‐06 5.0E‐06 6.8E‐06 3.0E‐05Mercury 2.60E‐04 lb/MMscf 7.8E‐07 3.4E‐06 4.7E‐06 2.0E‐05Nickel 2.10E‐03 lb/MMscf 6.3E‐06 2.7E‐05 3.8E‐05 1.6E‐04
Selenium 2.40E‐05 lb/MMscf 7.2E‐08 3.1E‐07 4.3E‐07 1.9E‐06TotalHAP 5.6E‐03 2.5E‐02 3.4E‐02 1.5E‐01
1.NaturalgasemissionfactorsfromAP‐42,Tables1.4‐3and1.4‐4
PollutantNaturalGasEmissionFactor1
Units
EmissionsperHeaterEmissionsforAll
Heaters
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TableN‐27.CoolingTower/BoilerFeedwater/WastewaterPretreatmentEmissions
Material Projected Usage (kg /year) Volatile Content Potential VOC emissions Potential HAP emissions(tpy) (tpy)
Nalco 3DT 265 49,932 0% 0.0 --Nalco 7320 112,347 10% 12.4 --Nalco 7330 57,921 1% 5.1E-01 --
Nalco Stabrex ST70 500 0% 0.0 --
Nalco Nexguard 22310 17,100 0% 0.0 --Nalco 1720 4,100 0% 0.0 --Nalco 1820 280 40% 1.2E-01 --
Sodium hypochlorite 4,380 N/A 4.0E-03 4.0E-0313.0 4.0E-03
Cooling Tower Water
Boiler Feedwater
Recycle Water Disinfection
Total
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TableN‐28.Utilities‐InkUsage‐Emissions
AnnualInkUsage1 VOCContent2 AnnualInkUsage1 VOCContent2 HAPContent3
(lb/yr) (%) (lb/yr) (%) (%) (lb/hr) (tpy) (lb/hr) (tpy)SoapMakingBusinessA&B 0 35 1,000 16 16 1.8E‐02 8.0E‐02 1.8E‐02 8.0E‐02DryConsumerProductsA 1,100 35 1,000 16 16 6.2E‐02 2.7E‐01 1.8E‐02 8.0E‐02Customization 330 16 ‐‐ ‐‐ ‐‐ 6.0E‐03 2.6E‐02 ‐‐ ‐‐Total 0.09 0.38 0.04 0.16
3.AssumesallVOCinthecodedaterinkisHAP.HAPisaglycolether.
VOCEmissions2 HAPEmissions3
1.ConservativeassumptionbasedonProcterandGambledesigndata.
2.Conservativelyassumedthattheinkcompositionis100%VOCandthatallinkislosttotheatmosphereduringusage.
BusinessUnit
CasePrintingInk CodeDaterInk
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TableN‐29.FinishedProductPackingEmissionsfromHotMeltGlue
AnnualGlueUsage1 VOCEmissionFactor HAPEmissionFactor(lb/year) (lb/lb) (lb/lb) (lb/hr) (tpy) (lb/hr) (tpy)
Soap Making Business A&B 438,000 3.0E‐02 1.3E‐01 1.0E‐03 4.4E‐03DryConsumerProductsA 250,080 1.7E‐02 7.5E‐02 5.7E‐04 2.5E‐03
Customization 2,000 1.4E‐04 6.0E‐04 4.6E‐06 2.0E‐054.7E‐02 2.1E‐01 1.6E‐03 6.9E‐03
1.ConservativeassumptionbasedonProcterandGambledesigndata.
2.ConservativelyassumedthatalloftheVOCinthehotmeltglueisvinylacetate.
BusinessUnitVOCEmissions HAPEmissions2
6.00E‐04 2.00E‐05
Total:
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TableN‐30.Utilities‐RoadParameter Value UnitIndustrialaugmentationfactor 1 dimensionlessNumberoftrafficlanes 2Surfacematerialsiltcontent1 3.3% %Surfacedustloading 125 lb/mile
DescriptionAverage Weight2 MilesperTrip2
MaximumTripsperHour
Maximum Trips per
Year(tons)
DeliveryTrucks 40 0.0417 30.8 365EmployeeVehicles 2 0.0417 0.5 365
(lb/hr) (tpy)DeliveryTrucks 5.0E‐04 2.2E‐03EmployeeVehicles 1.0E‐06 4.4E‐06
TOTAL 5.0E‐04 2.2E‐03
3.FromEmissionFactorDocumentationforAP‐42Section13.2.1, PavedRoads, Equation2‐2,assitedinWVDEPR‐13PermitFormAttachmentLforHaulRoads
PollutantUncontrolledTSPEmissions3
2.ConservativeassumptionbasedonProcterandGambledesigndata.
1.ConservativelyassumedtobeequaltoaveragefactorforAsphaltBatching,AP‐42Section13.2.1 PavedRoads ,Table13.2.1‐3
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TableN‐31.PlasticsMoldingSupplier‐EmissionsSummary
PM PM10 PM2.5 VOC HAPs NOX CO SO2 H2SO4RailCarUnloading 3.50E‐01 3.50E‐01 3.50E‐01 ‐‐ ‐‐ ‐‐ ‐‐ ‐‐ ‐‐StorageSilos 3.50 3.50 3.50 ‐‐ ‐‐ ‐‐ ‐‐ ‐‐ ‐‐PlasticRegrind 1.68E‐01 1.68E‐01 1.68E‐01 ‐‐ ‐‐ ‐‐ ‐‐ ‐‐ ‐‐FugitiveVOCEmissions ‐‐ ‐‐ ‐‐ 9.07 ‐‐ ‐‐ ‐‐ ‐‐ ‐‐SpaceHeaters 5.55E‐01 5.55E‐01 5.55E‐01 4.02E‐01 1.30E‐01 3.65 6.13 4.38E‐02 4.75E‐04CoolingTower 1.23 1.23 1.23 ‐‐ ‐‐ ‐‐ ‐‐ ‐‐ ‐‐Back‐UpGenerator 4.75E‐04 9.71E‐04 9.71E‐04 5.02E‐02 1.62E‐03 1.04E‐01 2.08E‐01 2.94E‐05 ‐‐
ProcessTotal 5.80 5.80 5.80 9.52 1.32E‐01 3.75 6.34 4.38E‐02 4.75E‐04
ActivityAnnualEmissions(tpy)
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EmissionFactors1
(lb/tonmaterial)
PM 7.00E‐02PM10 7.00E‐02PM2.5 7.00E‐02
(ton/yr) % (lb/hr) (tpy) (lb/hr) (tpy) (lb/hr) (tpy) (lb/hr) (tpy) (lb/hr) (tpy) (lb/hr) (tpy)21C RailcarUnload122C RailcarUnload223C RailcarUnload324C RailcarUnload425C RailcarUnload5
3.50 3.50 3.50 0.35 0.35 0.351.ConservativeProcterandGambleapproximation.Accountsforfiveunloadingpointsforrailcarswhichcanfeedanyof24storagesilos.
TOTAL
PM10 PM2.5
ControlEfficiencyControlDevice
Number
100,000 90% 0.80 3.50 0.80 3.50 0.80 3.50
TableN‐32.PlasticsMoldingSupplier‐RailcarUnloadingtoSilo‐EmissionFactors
TableN‐33.PlasticsMoldingSupplier‐RailcarUnloadingtoSilo‐Emissions
EmissionDescription
1.EstimatedusingaveragedustingfactorforalltypesofpelletstorageidentifiedbyEPA.ConservativelyassumesPM=PM10=PM2.5.
Operation
UnloadThroughput1
ControlledEmissionsPM PM10 PM2.5
UncontrolledEmissionsPM
0.357.99E‐02 0.35 7.99E‐02 0.35 7.99E‐02
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EmissionFactors1
(lb/tonmaterial)
PM 7.00E‐02PM10 7.00E‐02PM2.5 7.00E‐02
(ton/yr) % (lb/hr) (tpy) (lb/hr) (tpy) (lb/hr) (tpy)222S PelletStorage1223S PelletStorage2224S PelletStorage3225S PelletStorage4226S PelletStorage5227S PelletStorage6228S PelletStorage7229S PelletStorage8230S PelletStorage9231S PelletStorage10232S PelletStorage11233S PelletStorage12234S PelletStorage13235S PelletStorage14236S PelletStorage15237S PelletStorage16238S PelletStorage17239S PelletStorage18240S PelletStorage19241S PelletStorage20242S PelletStorage21243S PelletStorage22244S PelletStorage23245S PelletStorage24
3.5 3.5 3.51.ConservativeProcterandGambleapproximation.Storagesilosmaybefedfromanyoffiverailcarunloadingpoints.
TOTAL
PM PM10 PM2.5
100,000 0% 7.99E‐01 3.50 7.99E‐01 3.50 7.99E‐01 3.50
TableN‐34.PlasticsMoldingSupplier‐SiloStorage‐EmissionFactors
EmissionDescription
1.EstimatedusingaveragedustingfactorforalltypesofpelletstorageidentifiedbyEPA.ConservativelyassumesPM=PM10=PM2.5.
TableN‐35.PlasticsMoldingSupplier‐SiloStorage‐Emissions
EmissionUnit Operation
UnloadThroughput1
ControlEfficiency
UncontrolledEmissions
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EmissionFactors1
(lb/tonmaterial)
PM 2.10E‐01PM10 2.10E‐01PM2.5 2.10E‐01
(ton/yr) % (lb/hr) (tpy) (lb/hr) (tpy) (lb/hr) (tpy) (lb/hr) (tpy) (lb/hr) (tpy) (lb/hr) (tpy)246 PlasticRegrind 32,000 95% 0.77 3.36 0.77 3.36 0.77 3.36 3.84E‐02 1.68E‐01 3.84E‐02 1.68E‐01 3.84E‐02 1.68E‐01
3.36 3.36 3.36 1.68E‐01 1.68E‐01 1.68E‐011.ConservativeProcterandGambleapproximationof32%oftotalplasticthroughput.
TOTAL
ControlledEmissionsPM PM10 PM2.5 PM PM10 PM2.5
TableN‐36.PlasticsMoldingSupplier‐PlasticRegrind‐EmissionFactors
EmissionDescription
1.EstimatedusingaveragedustingfactorforalltypesofpelletstorageidentifiedbyEPA,multipliedby3xtoaccountforregrindprocess.ConservativelyassumesPM=PM10=PM2.5.
TableN‐37.PlasticsMoldingSupplier‐PlasticRegrind‐Emissions
EmissionUnit OperationThroughput1
ControlEfficiency
UncontrolledEmissions
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VOCEmissionFactors(lb/tonmaterial)
Forming1 0.0614
IsopropylAlcohol2 2000PartsWashing
CleaningSolvent2 2000
(ton/yr) (lb/hr) (tpy)247S Forming 100,000 0.70 3.07248S PartsWashing/ProcessCleaning 6 1.37 6.00
TOTAL 2.07 9.071.ConservativeProcterandGambleapproximation.
TableN‐38.PlasticsMoldingSupplier‐Cleaning‐EmissionFactorsEmissionDescription
2.Assumes100%lossrate.
TableN‐39.PlasticsMoldingSupplier‐Cleaning‐Emissions
EmissionUnit OperationUnloadThroughput1
UncontrolledEmissions
VOC
1.MichiganDepartmentofEnvironmentalQuality,"PlasticsProductionandProductsManufacturing"factsheet,emissionfactorformoldingmachine.
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TableN‐40.Utilities‐PMSHeaters‐Parameters
Value249S SpaceHeater1 5250S SpaceHeater2 5251S SpaceHeater3 2.5252S SpaceHeater4 2.5253S SpaceHeater5 1254S SpaceHeater6 1
171468,7601,020
TableN‐41.Utilities‐PMSHeaters‐CriteriaEmissions
NOX 50 lb/MMscf 1 0.83 3.65
CO 84.00 lb/MMscf 1 1.40 6.13
PM 7.60 lb/MMscf 1 1.27E‐01 5.55E‐01
PM10 7.60 lb/MMscf 1 1.27E‐01 5.55E‐01
PM2.5 7.60 lb/MMscf 1 1.27E‐01 5.55E‐01
SO2 0.60 lb/MMscf 1 1.00E‐02 4.38E‐02
VOC 5.50 lb/MMscf 1 9.17E‐02 4.02E‐01
H2SO4 6.50E‐03 lb/MMscf 2 1.08E‐04 4.75E‐04
EquivalentGasHours: Hoursat100%LoadNaturalGasHeatingValue(HHV):
Parameter Unit
TotalHeatInput: MMBtu/hrAnnualGasUsage: MMscf/yr
MMBtu/hrMMBtu/hrMMBtu/hrMMBtu/hrMMBtu/hrMMBtu/hr
Btu/scf
1.NaturalgasemissionfactorsfromAP‐42Section1.4.PMassumedtoequalPM10.
2.Naturalgasfactorcalculatedassuming1%ofsulfurbecomesH2SO4.FueloilemissionfactorfromEmergencyPlanningandCommunityRight‐To‐KnowAct,EPCRA‐Section313:GuidanceforReportingSulfuricAcid(acidaerosolsincludingmists,vapors,gas,fog,andotherairborneformsofanyparticlesize).(March1998)EPA‐745‐R‐97‐007.
PollutantNaturalGas
EmissionFactorUnits Reference
NaturalGasHourly
Emissions(lb/hr)
NaturalGasAnnual
Emissions(tpy)
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TableN‐42.Utilities‐PMSHeaters‐ParametersValue Unit17 MMBtu/hr
8,260 hr/yr1,020 Btu/scf
TableN‐43.Utilities‐PMSHeaters‐HAPEmissions
lb/hr tpy
2‐Methylnaphthalene 2.4E‐05 lb/MMscf 4.00E‐07 1.65E‐063‐Methylchloranthrene 1.8E‐06 lb/MMscf 3.00E‐08 1.24E‐07
7,12‐Dimethylbenz(a)anthracene 1.6E‐05 lb/MMscf 2.67E‐07 1.10E‐06Acenaphthene 1.8E‐06 lb/MMscf 3.00E‐08 1.24E‐07Acenaphthylene 1.8E‐06 lb/MMscf 3.00E‐08 1.24E‐07Anthracene 2.4E‐06 lb/MMscf 4.00E‐08 1.65E‐07
Benz(a)anthracene 1.8E‐06 lb/MMscf 3.00E‐08 1.24E‐07Benzene 2.1E‐03 lb/MMscf 3.50E‐05 1.45E‐04
Benzo(a)pyrene 1.2E‐06 lb/MMscf 2.00E‐08 8.26E‐08Benzo(b)fluoranthene 1.8E‐06 lb/MMscf 3.00E‐08 1.24E‐07Benzo(g,h,i)perylene 1.2E‐06 lb/MMscf 2.00E‐08 8.26E‐08Benzo(k)fluoranthene 1.8E‐06 lb/MMscf 3.00E‐08 1.24E‐07
Chrysene 1.8E‐06 lb/MMscf 3.00E‐08 1.24E‐07Dibenzo(a,h)anthracene 1.2E‐06 lb/MMscf 2.00E‐08 8.26E‐08
Dichlorobenzene 1.2E‐03 lb/MMscf 2.00E‐05 8.26E‐05Fluoranthene 3.0E‐06 lb/MMscf 5.00E‐08 2.07E‐07Fluorene 2.8E‐06 lb/MMscf 4.67E‐08 1.93E‐07
Formaldehyde 7.5E‐02 lb/MMscf 1.25E‐03 5.16E‐03Hexane 1.8E+00 lb/MMscf 3.00E‐02 1.24E‐01
Indeno(1,2,3‐cd)pyrene 1.8E‐06 lb/MMscf 3.00E‐08 1.24E‐07Naphthalene 6.1E‐04 lb/MMscf 1.02E‐05 4.20E‐05Phenanathrene 1.7E‐05 lb/MMscf 2.83E‐07 1.17E‐06
Pyrene 5.0E‐06 lb/MMscf 8.33E‐08 3.44E‐07Toulene 3.4E‐03 lb/MMscf 5.67E‐05 2.34E‐04Arsenic 2.0E‐04 lb/MMscf 3.33E‐06 1.38E‐05Beryllium 1.2E‐05 lb/MMscf 2.00E‐07 8.26E‐07Cadmium 1.1E‐03 lb/MMscf 1.83E‐05 7.57E‐05Chromium 1.4E‐03 lb/MMscf 2.33E‐05 9.64E‐05Cobalt 8.4E‐05 lb/MMscf 1.40E‐06 5.78E‐06Lead 5.0E‐04 lb/MMscf 8.33E‐06 3.44E‐05
Manganese 3.8E‐04 lb/MMscf 6.33E‐06 2.62E‐05Mercury 2.6E‐04 lb/MMscf 4.33E‐06 1.79E‐05Nickel 2.1E‐03 lb/MMscf 3.50E‐05 1.45E‐04
Selenium 2.40E‐05 lb/MMscf 4.00E‐07 1.65E‐06TotalHAP 3.15E‐02 1.30E‐01
ParameterHeatInput:
HoursofOperationonNaturalGas:NaturalGasHeatingValue(HHV):
EmissionsperHeater
1.NaturalgasemissionfactorsfromAP‐42,Tables1.4‐3and1.4‐4
PollutantNaturalGas
EmissionFactor1Units
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Attachment NTabler Station
TableN‐44.Utilities‐PMSCoolingTower‐Emissions
Parameter Value
EmissionUnit 255S
Location1 BBS
FlowRate(gpm) 7,000
OperatingHours(hr/yr) 8,760
DensityofWater(lb/gal) 8.35
TotalDissolvedSolids,TDS(ppm) 1,600
Drift(%)2 5.00E‐03
Drift(gpm) 0.35
PM/PM10/PM2.5(lb/gal)3 6.68E‐07
PM/PM10/PM2.5(lb/hr) 2.80E‐01
PM/PM10/PM2.5(tpy) 1.23
1.Clientspecification.
2.DriftPercentageforInducedDraftCoolerspecifiedinemailfromBrianMensinger(TrinityConsultants)toAllisonCole(TrinityConsultants)onJuly22,2015.3.PM10areconservativelyoverestimatedby(TDS,ppm)x(TotalDriftRate,
lb/gal)/106,basedonAP‐42Section13.4‐3.
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Attachment NTabler Station
TableN‐45.PlasticsMolding‐Back‐UpGenerator
SourceDesignation: Engine Generator
EmissionUnit: 256S ‐‐
Manufacturer:1 ‐‐ Generac
StrokeCycle: 4‐stroke ‐‐
TypeofBurn:1 Rich ‐‐
FuelUsed: NaturalGas ‐‐
HigherHeatingValue(HHV)(Btu/scf): 1,020 ‐‐
PowerGenerated@2,300rpm(KW) ‐‐ 70
MaximumFuelConsumptionat100%Load(scf/hr):1 196 ‐‐
HeatInput(HHV)(MMBtu/hr):1 0.20 ‐‐
EmissionControls: None ‐‐
OperationalDetail Value
PotentialAnnualHoursofOperation(hr/yr): 500
PotentialFuelConsumption(MMscf/yr): 0.10
Pollutant EmissionFactors Units
NOX1 2.70 g/kw‐hr
CO1 5.40 g/kw‐hr
SO22 5.88E‐04 lb/MMBtu
PM(filterableonly)2 9.50E‐03 lb/MMBtu
PM10(filterable+condensable)2 1.94E‐02 lb/MMBtu
PM2.5(filterable+condensable)2 1.94E‐02 lb/MMBtu
VOC1 1.30 g/kw‐hr
Pollutant (lb/hr)3 (tpy)4
NOx 4.17E‐01 1.04E‐01
CO 8.33E‐01 2.08E‐01
SO2 1.18E‐04 2.94E‐05
PM 1.90E‐03 4.75E‐04
PM10 3.88E‐03 9.71E‐04
PM2.5 3.88E‐03 9.71E‐04
VOC 2.01E‐01 5.02E‐02
TableN‐45.PlasticsMolding‐Back‐UpGenerator
EmissionFactor
Pollutant (lb/MMBtu)2 (lb/hr)3 (tpy)4
Acetaldehyde 2.79E‐03 5.58E‐04 1.40E‐04
Acrolein 2.63E‐03 5.26E‐04 1.32E‐04
Benzene 1.58E‐03 3.16E‐04 7.90E‐05
1,3‐Butadiene 6.63E‐04 1.33E‐04 3.32E‐05
CarbonTetrachloride 1.77E‐05 3.54E‐06 8.85E‐07
Chlorobenzene 1.29E‐05 2.58E‐06 6.45E‐07
Chloroform 1.37E‐05 2.74E‐06 6.85E‐07
1,3‐Dichloropropene 1.27E‐05 2.54E‐06 6.35E‐07
Ethylbenzene 2.48E‐05 4.96E‐06 1.24E‐06
EthyleneDibromide 2.13E‐05 4.26E‐06 1.07E‐06
Formaldehyde 2.05E‐02 4.10E‐03 1.03E‐03
Methanol 3.06E‐03 6.12E‐04 1.53E‐04
MethyleneChloride 4.12E‐05 8.24E‐06 2.06E‐06
Naphthalene 9.71E‐05 1.94E‐05 4.86E‐06
PAH 1.41E‐04 2.82E‐05 7.05E‐06
Styrene 1.19E‐05 2.38E‐06 5.95E‐07
Toluene 5.58E‐04 1.12E‐04 2.79E‐05
1,1,2,2‐Tetrachloroethane 2.53E‐05 5.06E‐06 1.27E‐06
1,1,2‐Trichloroethane 1.53E‐05 3.06E‐06 7.65E‐07
VinylChloride 7.18E‐06 1.44E‐06 3.59E‐07
Xylenes 1.95E‐04 3.90E‐05 9.75E‐06
TotalHAP 6.48E‐03 1.62E‐03
1 EmissionfactorsfromCertificateofConformityGGNXB06.82C1‐043.Factorsfrom40CFR60,SubpartJJJJ,Table1.2
3
4 AnnualEmissions(tons/yr)=EmissionRate(lb/hr)×(MaximumAllowableOperatingHours,500hr/yr)×(1ton/2000lb).
EmissionRate(lb/hr)=RatedCapacity(MMBtu/hr)×EmissionFactor(lb/MMBtu)EmissionRate(lb/hr)=EmissionFactor(g/kw‐hr)*Capacity(KW)*ConversionFactor(lb/g)
PotentialEmissions
PotentialEmissions
EmissionfactorsfromAP‐42Section3.2,Table3.2‐3"UncontrolledEmissionFactorsfor4‐stroke,Rich‐burnEngines,"SupplementF,August2000.
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P&G – Tabler Station | R13 Permit Trinity Consultants
ATTACHMENT O
Monitoring/Recordkeeping/Reporting/Testing Plans
Attachment OTabler Station
PlanTypeEmissionunit
Pollutant Requirements FrequencyMethodof
MeasurementRegulatoryReference
TBD 1C SO2/H2SO4 MonitorpH Hourly TBD TBD
TBD 2C SO2/H2SO4 MonitorpH Hourly TBD TBD
TBD 3C PM/PM10/PM2.5 Monitorpressuredrop Weekly TBD TBD
TBD 4C PM/PM10/PM2.5 Monitorpressuredrop Weekly TBD TBD
TBD 5C PM/PM10/PM2.5 Monitorpressuredrop Weekly TBD TBD
TBD 6C PM/PM10/PM2.5 Monitorpressuredrop Weekly TBD TBD
TBD 7C PM/PM10/PM2.5 Monitorpressuredrop Weekly TBD TBD
TBD 8C PM/PM10/PM2.5 Monitorpressuredrop Weekly TBD TBD
TBD 9C PM/PM10/PM2.5 Monitorpressuredrop Weekly TBD TBD
TBD 10 PM/PM10/PM2.5 Monitorpressuredrop Weekly TBD TBD
TBD 11C PM/PM10/PM2.5 Monitorpressuredrop Weekly TBD TBD
TBD 12C PM/PM10/PM2.5 Monitorpressuredrop Weekly TBD TBD
TBD 13C PM/PM10/PM2.5 Monitorpressuredrop Weekly TBD TBD
TBD 14C AllPollutantsInitialComplianceDemonstration
TBD TBD TBD
TBD 14C HAP/VOCMonitorinternaltemperature
Hourly TBD TBD
TBD 14C HAP/VOCOperateRTOwhenLiquid
SoapAHotMixTankisbeingused.1
TBD TBD TBD
TBD 15C PM/PM10/PM2.5 Monitorpressuredrop Weekly TBD TBD
TBD 16C PM/PM10/PM2.5 Monitorpressuredrop Weekly TBD TBD
TBD 17C PM/PM10/PM2.5 Monitorpressuredrop Weekly TBD TBD
TBD 18C PM/PM10/PM2.6 Monitorpressuredrop Weekly TBD TBD
TBD 19C PM/PM10/PM2.5 Monitorpressuredrop Weekly TBD TBD
TBD 20C PM/PM10/PM2.5 Monitorpressuredrop Weekly TBD TBD
TBD 21C PM/PM10/PM2.5 Monitorpressuredrop Weekly TBD TBD
TBD 22C PM/PM10/PM2.5 Monitorpressuredrop Weekly TBD TBD
TBD 23C PM/PM10/PM2.5 Monitorpressuredrop Weekly TBD TBD
TBD 24C PM/PM10/PM2.5 Monitorpressuredrop Weekly TBD TBD
TBD 25C PM/PM10/PM2.5 Monitorpressuredrop Weekly TBD TBD
TBD 26C PM/PM10/PM2.5 Monitorpressuredrop Weekly TBD TBD
TBD 256S AllPollutants Non‐ResettableHourMeter Monthly TBD NSPSJJJJ
TBD 249S‐254S AllPollutants FuelUsage Monthly TBD TBDTBD 1S‐2S Dioxane Maintainrecords Monthly TBD NSPSVVa
TBD 196S‐199S AllPollutantsFuelRecords,including%
SulfurMonthly TBD NSPSDc
TBD 203S‐207S AllPollutantsFuelRecords,including%
SulfurMonthly TBD NSPSIIII
TBD 203S‐207S AllPollutants Non‐ResettableHourMeter Monthly TBD NSPSIIII
TBD 210S‐215S AllPollutants FuelUsage Monthly TBD TBD
AttachmentOMONITORING,RECORDKEEPING,REPORTING,ANDTESTINGPLANS
Monitoring,Recordkeeping,ReportingandTestingPlans.Attachproposedmonitoring,recordkeeping,reportingandtestingplansinordertodemonstratecompliancewiththeproposedemissionslimitsandoperatingparametersinthispermitapplication.ProvidethisinformationasAttachmentO.
*Pleasebeawarethatallpermitsmustbepracticallyenforceablewhetherornottheapplicantchoosestoproposesuchmeasures.Additionally,theDAQmaynotbeabletoacceptallmeasuresproposedbytheapplicant.Ifnoneoftheseplansareproposedbytheapplicant,DAQwilldevelopsuchplansandincludetheminthepermit.
1.Assumes24hours(per12‐monthrollingperiod)ofuncontrolledoperation.
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