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HomeMy WebLinkAboutAQ_F_1900015_20170627_EI_Cmb-EI-File 2016 Emissions Inventory Review / Data Tracking Form Facility Name: Arauco Panels USA, LLC Facility ID: 1900015 Facility Assigned to: Data Entry: Chatham County Classification: Matthew Mahler Confidential Copy Submitted? Title V �° —��- �� ❑E S NO Initial Review/Data Entry Enter date received into ED. Date Received: 6 —Z.7— 17 ❑ Assigned to appropriate individual. Date Assigned: Date Due: ❑ Paper copy submitted: One copy received with supporting documentation,certification form signed by responsible official,and /appears generally complete;OR 12 Electronic copy submitted: All supporting documentation and certification form(with time/date stamp)signed by responsible official has been received. i o x,'c pa I luf-etn't- an J �� Comments: C ri f f- C, n o l(�t-�h-i- r e duc_fi,'„- s rs wt�in l,� a� a��h.fi e ct 40 less ove^ c1r,ej +*Ins +� . nRv��tile_b oGrd d4-44-rs in 2616. I�i f UA ,� �cr.{�SsT o ^ ?n cv easesy Clue MM6+,J fvf- cF ffegi fuel &,d Sander'clas-f- Celti.hJSi�ot7 Fkff-f,`cte— hoa.-<L P laht. Inventory Review 211�All forms and supporting documentation appear to be complete if paper submission(check ED OS data if electronic). Contact,address,phone number changes entered into I-Beam/Facilities if necessary. p� All known operating scenarios,control devices,and emission release points have been entered for each emission source(permitted, insignificant,and unpermitted)or note that the emission source was not operated or not required to report. C� Check if SCC codes for each OS are accurate and update if needed. l Evaluate"U"sources for significance and address according to policy. Calculations/forms appear to add up correctly. All compliance issues are being addressed(e.g.Toxics limits,above TV thresholds,large emissions increase/decrease,installation without a permit). Er All volatile HAPs/TAPs were included in the VOC total. GY Calculations and control efficiencies appear correct. Emission factors are the best available and most current factors appropriate for the reporting facility(e.g. stack testing,AP-42,etc.). La'Review facility comments and address any issues. Cr Update ED(Data Entry Main)if additional information is required(corrections due date and date received). R"Check all ED QA/QC reports. IV Comparison with previous emission inventory must be made and outliers(> 10%)must be investigated and explained. 61"'Put inventory review comments and summarize any changes in ED-Data Entry Main"DAQ internal comments". Print and attach the facility total report. Date Info Requested: Date Info Received: Total Days on Hold: Date Review Complete: ^ Signature: Date Submitted to EI Coordinator: f 0-2-Y 17 Date Approved: Initials: JAIN i Facility Total CY 2016 Emission Summary Recorded in ED Facility ID#: 1900015 f Facility Name: Arauco Panels USA,LLC Permit#(s): 03449T47 Green House Gases Pollutants(GHG) Actual Emissions Tons/Yr Pollutant. CAS Demini- Change mus Not Not N/A Reported Reported CO2 equivalent(sum of individual GHG pollutant emission No GHGs times their 1995 IPCC Global Warming Potential(GWP), Reported converted to'metric tons) Criteria Pollutants Actual Emissions (Tons/Year) Pollutant CAS CY 2016 CY 2015 Demini- % from ED from Fees mus Change CO CO 389.07 518.43 0.5 -25.0% NOx NOx 241.64 296.93 0.5 -18.6% PM(TSP) TSP 126.44 185.68 0.5 -31.9% PM10 PMIO 123.90 182.48 0.5 -32.1% PM2.5 PM2 5 111.67 166.90 0.5 -33.1%- S02 3O2 14.52 12.64 0.5 14.9% VOC VOC 597.49 793.10 0.5 -24.7% Hazardous Air Pollutants(HAPs) Actual Emissions and/or Toxic Air Pollutants(TAPs) (Pounds/Year) Pollutant CAS CY 2016 CY 2015 Demini- % from ED from Fees mus Change Arsenic& Compounds(total mass of elemental AS,arsine and 1.31 1.26 0.01 I 4,0% all inorganic compounds) Arsenic Compounds-Arsine gas(Component of 7784-42-1 Not 0.983000 0.01 N/A ASC) Reported Arsenic Unlisted Compounds- Specify Compound ASC-Other 1.31 0.278600 0.01 370.3% (Component of ASC) Cadmium&compounds(total mass includes elemental metal) 1.23 1.27 0.1 -3.1 Cadmium Metal,elemental,unreacted(Component of 7440-43-9 1.23 1.27 0.1 -3.8% CDC) Chromium-All/Total(includes Chromium(VI) categories, 3.81 3.65 0.1 4.4% metal and others) Chromic acid(VI)(Component of So1CR6&CRC) 7738-94-5 0.286500 0.123000 0.01 132.9% 10/25/2017 Pagel of 4 Facility Total CY 2016 Emission Summary Recorded in ED Facility ID#: 1900015 t ^ Facility Name: Arauco Panels USA,LLC Permit#(s): 03449T47 Hazardous Air Pollutants(HAPs) Actual Emissions and/or Toxic Air Pollutants(TAPs) (Pounds/Year) Pollutant CAS CY 2016 CY 2015 Demini- % from ED from Fees mus Change Chromium(VI)Non-Specific Unlisted Compounds- NSCR6-Other Not 0.126000 0.01 N/A Specify Compound(Component of NSCR6&CRC) Reported Chromium Unlisted Compounds-Specify Compound CRC-Other 3.52 3.40 0.1 3.6% (Component of CRC) F omium(VI)Non-Specific Compounds,as Chrom(VI) Not 0.126000 0.01 NIA mponent CRC) Reported Chromium(VI)Non-Specific Unlisted Compounds- NSCR6-0ther Not 0.126000 0.01 N/A Specify Compound(Component of NSCR6&CRC) Reported Chromium(VI)Soluble Chromate Compounds(Component of 0.286500 0.123000 0,01 I 132.9% CRC) Chromic acid(VI)(Component of So1CR6&CRC) 7738-94-5 0.286500 0.123000 0.01 132.9% Lead&compounds 11.88 12.05 1.0 -1.4% Lead Unlisted Compounds- Specify Compound PBC-other 11.88 12.05 10.0 -1.4% (Component of PBC) Manganese& compounds 33.10 27.50 10,0 20.4% Manganese Unlisted Compounds-Specify Compound MNC-Other 33.10 27.50 10.0 20.4% (Component of MNC) Mercury& Compounds-all total mass includes Hg Vapor 0.633600 0.576400 0.001 9.9% Mercury,vapor(Component of HGC) 7439-97-6 0.633600 0.576400 0.001 9.9% Nickel& Compounds,sum total mass includes elemental 4.02 3.43 1.0 17.2% Nickel metal(Component of NIC) 7440-02-0 4.02 3.43 1.0 17.2% Polycyclic Organic Matter(7 PAH Compounds for NIF) 1.45 1.39 1.0 4.3% Benzo(a)pyrene(Component of 83329/POMTV& 50-32-8 1.45 1.39 1.0 4.3% 56553/7PAH) Polycyclic Organic Matter(Specific Compounds from OAQPS 68.51 62.59 1.0 9.5% or TP9 Benzo(a)pyrene(Component of 83329/POMTV& 50-32-8 1.45 1.39 1.0 4.3% 56553/7PAH) Naphthalene(Component of 83329/POMTV) 91-20-3 67.06 61.20 1.0 9.6% Acetaldehyde 75-07-0 5,485.00 7,979.12 10.0 -31.3% 10/25/2017 Page 2 of 4 j Facility Total CY 2016 Emission Summary Recorded in ED Facility ID#: 1900015 I' Facility Name: Arauco Panels USA,LLC Permit#(s): 03449T47 Hazardous Air Pollutants(HAPs) Actual Emissions and/or Toxic Air Pollutants(TAPS) (Pounds/Year) Pollutant CAS CY 2016 CY 2015 Demini- % from ED from Fees mus Change Acrolein 107-02-8 1,534.15 2,243.59 10.0 -31.6% Benzene 71-43-2 267.50 234.50 1.0 14.1% Bromine 7726-95-6 12.80 Not 10.0 N/A Reported Carbon tetrachloride 56-23-5 7.05 6.73 1.0 4.8% Chlorine 7782-50-5 416.00 367.30 100.0 13.3% Cumene 98-82-8 490.00 707.00 100.0 -30.7% Ethylene dichloride(1,2-dichloroethane) 107-06-2 17.74 17.72 1.0 0.1% Formaldehyde 50-00-0 255,023.10 66,126.70 10.0 285.7% Hexachlorodibenzo-p-dioxin.1,2,3,6,7,8 57653-85-7 0.980100 0.978000 0.00001 0.2% Hexane,n- 110-54-3 341.00 305.00 100.0 11.8% Hydrogen chloride(hydrochloric acid) 7647-01-0 958.00 851.00 100.0 12.6% MEK(methyl ethyl ketone,2-butanone) 78-93-3 1,390.00 1,680.29 100.0 -17.3% Methanol(methyl alcohol) 67-56-1 46,400.00 81,546.00 1,000.0 -43.1% Methyl bromide(bromomethane) 74-83-9 8.50 9.28 1.0 -8.4% Methyl chloride(chloromethane) 74-57-3 14.13 14.07 1.0 0.4% Methylene chloride 75-09-2 398.60 348.80 1.0 14.3% MIBK(methyl isobutyl ketone) 108-10-1 202.00 245.00 10.0 -17.6% Phenol 108-95-2 1,834.00 3,253.06 100.0 -43.6% Phosphorus Metal,Yellow or White 7723-14-0 60.34 60.15 1.0 0.3% Polycyclic Organic Matter(Inc PAH,dioxins,etc.NC POM 167.94 83.07 1.0 102.2% &AP 42 historic) Propionaldehyde 123-38-6 437.00 637.81 10.0 -31.5% Propylene dichloride(1,2-dichloropropane) 78-87-5 18.50 17.60 10.0 5.1% Selenium Compounds SEC Not 0.988000 10.0 N/A Reported Styrene 100-42-5 Not 33.70 100.0 N/A Reported 10/25/2017 Page 3 of 4 Facility Total CY 2016 Emission Summary Recorded in ED Facility ID#: 1900015 Facility Name: Arauco Panels USA,LLC Permit#(s): 03449T47 + Hazardous Air Pollutants(HAPs) Actual Emissions and/or Toxic Air Pollutants(TAPS) (Pounds/Year) Pollutant CAS CY 2016 CY 2015 Demini- % from ED from Fees mus Change TCE(trichloroethylene) 79-01-6 Not 10.40 1,000.0 N/A Reported Toluene 108-88-3 Not 12.50 100.0 N/A Reported Trichlorophenol,2,4,5- 95-95-4 Not 0.146000 10.0 N/A Reported Vinyl chloride 75-01-4 11.28 11.24 0.1 0.3% Xylene(mixed isomers) 1330-20-7 Not 2.79 100.0 N/A Reported Largest Individual HAP Formaldehyde 255,023.10 lbs Total HAP Emissions 314,216.32 lbs Largest Individual CAP VOC 597.49 tons Total CAP Emissions 1,366.62 tons Total TAP Emissions 267,939.91 lbs Total Aggregate 1,367.51 tons Emissions DAO's Comments Regarding Inventory Criteria,toxic,and HAP pollutant reductions are attributed mainly to less oven dried tons in particleboard dryers in 2016. Toxic/HAP emission increases due to higher MMBtu/yr combustion of Hog fuel and Sanderdust combustion in Particle Board plant. Increase in formaldehyde emissions are from a change in emission factor(1.18 lb/ODT)due to the shutdown of the Photo gas chemical treatment(PGT)of MDF Plant Dryer on October 23,2.015 due to a Special Order of Consent(SOC)received by facility. According to NCDAQ policy,for OS-51,Arsenic Compounds-Arsine gas and Chromium(VI)Non-Specific were recoded to ASC-Other and Chromic Acid(VI)(7738945),respectively. 10/25/2017 Page 4 of 4 ✓n t.m _ COPY of RECORD Date Submitted: 6/27/2017 09:11 :27 z Inventory Certification Form(Title V) n Facility Name: Arauco Panels USA,LLC Facility ID : 1900015 985 Corinth Road Permit : 03449 0 t_ o Moncure,NC 27559 County : Chatham °�°- C r DAQ Region :RRO N < o North Carolina Department of Environment and Natural Resources Division of Air Quality .v Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 0 `= These forms must be completed and returned even if the facility did not operate or emissions were i@ro The legally defined "Responsible Official"of record for your facility is Tom Ouesenberry This person or one that meets the definition below must sign this certification form. The official submitting the information must certify that he/she complies with the requirements as specified in Title 15A NCAC 2Q.0520(b)which references and follows the federal definition.40 CFR Part 70.2 defines a responsible as meaning one of the following: 1.For a corporation: a president,secretary,treasurer,or vice—president of the corporation in charge of a principal business function,or any other person who performs similar policy or decision making functions for the overall operation of one or more manufacturing,production,or operating facilities applying for a or subject to a permit and either i.the facilities employ more than 250 persons or have gross annual sales or expenditures exceeding$25 million(in second quarter 1980 dollars); or ii. the delegation of authority to such representatives is approved in advance by the permitting authority; 2.For partnership or sole propietorship;a general partner or the proprietor,respectively; 3.for a muncipality,state,federal,or other public agency includes the chief executive officer having responsibility for the overall operations of a principal geographic unit of the agency(e.g.,a Regional Administrator of EPA). CERTIFICATION STATEMENT: certify that I am the responsible official for this facility,as described above, and hereby certify that the information contained in this air emissions report, including attached calculations and documentation,is true,accurate and complete. (Subject to legal nalities of up to$25,000 per occurrence and possible imprisonment as outlined in G.S.§143-215.3(a)(2)) Responsible Official's Signature Below use blue ink): Date Signed: Printed Name: Tom Queessenberry -Sign ture: This form applies to Title V facilities. If this facility is not classified as Title V,please telephone your regional office Emission Inventory contact at once for proper forms. Email address of Responsible Official: Tom.Quesenberry@flakeboard.com Information on this Form cannot be held confidential COPY of RECORD Date Submitted: 6/27/2017 09:11:27 1 �rA N;k �T V 79��74 AM?9 V"�Mw 777 w7M W977 I I 7T Rl"Mk ROM N7ml Wn R _*M ANNUAL ACTIVITY AND USAGE INFORMATION ARAUCO PANELS USA LLC-MONCURE,NORTH CAROLINA 2016 PS Production Data 2016 PB Plant Production Data Total Natural Gas Usage from PSNC website 1650679 ccf Activity and Usage 2016 Annual Amount Activity and Usage 2016 Annual Amount Descri tion Total Plant Description Without PGT running PRESS AND BAGFILTERS PB Production 7 m' PB Production m' PB Production 115,372 MSF 3 4"inch PB Production 215,372 MSF 3 4"inch Wood processedb mill 136,575 EDT Wood Processedb mill 136575 BDT Press Abort Operating Hours 27 hours/year Operating Hours hours/year Hog Fuel Combusted in Wellons: 0 Ibs/ear Wellons Bypass Sanderdust Combusted in Dryers: 60,469,794 Ibs ear Wellons Gas Firing MMScf r Backup Natural Gas Usage in Dryers: 16.51 MMSCF/r Wellons Burner Hours 12.0 hours/ear Activity and Usage 201S Annual Amount Fire Pump Engine Op.Hours hours ear Description With PGT running Backup Generator 0 .Hours 1L2 hours/year hours/year PB Production 0 m' Gasoline Tank allons/ear P8 Production 0 MSF 3/4"inch Total VOC Emissions 11 Ibs Wood rocessedb mill 0 BDT LaminatingPresses TFl O eratin Hours 4,778 hours/year Wemhoner Operating Hours 5,938 hours ear Wemhoner Annual Production 0,241 m' Wemhoner Annual Production 26,755 MSF Board Feet Steinemann Operating Hours 0 hours/year Steinemann Annual Production 0 m' Steinemann Annual Production 0 MSF Board Feet Thermal oil heater Natural Gas Usage 6.602 MMSCF r TFL Diesel Usage 0 al r TFL=935260 panels at avg 40 sqft 2016 MDF Production Data 272120 Total Natural Gas Usage from PSNC website ccf 30235.55556 191205 Activity and Usage 2016 Annual Amount Descri Lion Total Plant Lo Procsin Line Lo Throues h ut 0.0 tons ear 5049 Op hrs in 2015 Chi Throughput 0 tons/year Bark Throughput 0.0 tons/year New MDF Plant Cyclones and Ba houses MDF Prod m3 Sander Prod m3 Annual press Production: 272,230 m' 74493 MDF and 43904 HDF in 2015 174997.7 165,574 Refiner Abort C clone O,ration Hours 157 hr/r 98894.25223 93569.75501 Fiber slher s stem filter O¢ration Hours 7191 hr r Press production Hrs For Line Clean-U Filter O¢ration Hours 7,191 hr/r Press production Hrs Press prod hrs Sander Prod Hrs Mat reect system Filter O¢ration Hours 502 hr/r Press production Hrs 6145 3897 Saws stem r0¢ration Hours 7,191 hr r Press production Hrs Sanders steFiltem No.I Exhaust Filter Operation Hours 565 hr/r total sander production hrs Rec cled Fiber Silo No.1 Filter Operation Hours 502.0 hr/r 10%of press production Sanders stem No.I Exhaust Filter O eraton Hours 5,651 hr/r total sander production hrs Sander Dust Silo No.1 Filter O eration Hours 2,826 hr/r total sander production hrs D Sawdust Silo Filter O eration Hours 1,191 hr r Press production Hrs Rec cled Fiber Silo No.2 Filter O eration Hours 0.0 hr r 2%of press production hrs Sander Dust Silo No.2 Filter Operation Hours 2,826 hr r total sander production hrs MDF Teaford Total Annual Teaford Energy Production mmbtu r Press production hrs Ho Fuel Combusted in Teaford: 59,137,142 Ib r 1 72436 MMBTU/yr for Teaford 9.333333333 Sanderdust Combusted in Teaford: 11,264,218 Ib r MDF Press and D er Scrubbers Scrubber controllin Press Operation Hours 7,191 hr/r Press production hrs Teaford Abort Hours: 638 hr r Annual Press Production: 198,728 ODT r Annual Refiner(Dryer)Production: 198,728 ODT r Annual Sander Production: 339,755 ODT/r Annual Sander Production: 272,230 MSF 3 4"/r D er Scrubber O eration Hours 7,191 hr/r Total Backup Natural Gas Fired Burner Capacity(ES-02C an. Backu natural as-Rred dr er burners 89.08 mmscf/r Total Thermal Oil Heater Natural Gas Fired Burner Capacity(ES-18,11 Backu Natural Gas Burnen-Hot Oil Total Natural Gas Burnei #of Burners: 3 a Burner Natural Gas Use: 67.16 mmscf/r Backup Diesel Generator Generator Run Time: 27 hr r Fu hive Emissions:Resin Tanks #Resin Tanks in O eration: 3# Sanderdust burned in Teaford Fu hive Emiss(ons:Ponds and Spray Fields 165,574 Gallons lrri ated: 1 943000 al r See individual spreadsheet cwu+vcaynueW�.+ouruRm.amwmao.a.r.mw.h mmn.nn tomm owwo.uo,tszucun�c P.,..w30e.si Cak.fwnt mrama e.c B-2 WI-11 MDF Plant Log Processing Line The revised MDF project includes a new log processing line. Logs will be debarked and chipped. The chipper is in an enclosed building and there are no PM emissions. Emissions from log debarking are estimated below. Emissions from transport of bark and chips to piles are also estimated below. Log Throughput: 0 tons/yr Chip Throughput: 0 tons/yr Bark Throughput: 0 tons/yr Log Debarking Emissions Compound Emission Factor Potential Emissions Ib/ r ton/ r PM 0.0024 Ib/ton log 0.00E+00 0.00E+00 PM-10 0.00048 Ib/ton log 0.00E+00 0.00E+00 No PM2.5 emissions are expected from log debarking There are no log debarking emission factors in the current version of AP-42. Log debarking factor is estimated at 10%of 0.024 lb PM/GT logs in 1980 AP-42 Plywood section,table 10.3-1(Rated E). PM-10 is estimated as 30%of total PM. This emission factor is used by similar sources in NC for the purpose of air emissions inventories. Chip and Bark Handling Emissions The factor for chip/bark conveying and drops is determined using the predictive equation found on page 13.2.4-3(Aggregate Handling and Storage Piles-Section 13.2.4)of AP-42,11/06 edition. The equation takes into account particle size,wind speed,and material moisture content. An average wind speed of 15 mph is used. The value for particle size,k @<30 um is given as 0.74. A 50%moisture content is used for chips and bark. The equation is given as where E is the emission factor,U is the wind speed, M is the moisture content and k is the particle size: E=k(0.0032)*QU/511.3/(M/2)14) lb/ton PM E= 1.09E-04 lb/ton PM10 E= 5.16E-05 lb/ton or 47.3%of PM Compound Emission Factor Potential Emissions Ib/yr ton/yr Chi Handling PM I 1.09E-04 Ib/ton chips I 0.00E+00 I0.00E+00 PM-10 I 5.16E-05 Ib/ton chips I 0.00E+00 0.00E+00 Bark Handlin PM I 1.09E-04 Ib/ton bark I 0.00E+00 0.00E+00 PM-10 I 5.16E-05 Ib/ton bark I 0.00E+00 0.00E+00 No PM2.5 emissions are expected from chip and bark handling 4 o N 66 y a g m ry o O A �COOe'e000000 0 0 0 0 0 0 0 0 0 0 0 w N n O V�O C 'I Cod 6d6 E� C r m$m sa N mdt�+l�V Q 5' N`fFHuu/-u. d0i 000.�iGm o0 r - o0000000go �.� .E. om m 4 4 6 4 6 6 W W f. o ��nrLL��uu�u t c3 pry Am e ;OOOO�aaaaaa 2 `nn.7 N.ry.rvi.rv-im�od �w ry Hti1 mb oo.0O.b 11 a 64 E L a a a a a 0 a 0 0 0 0 & ________ " o o w ftO O D O O O D O y a.6 v z h rmmnonnnmoom Io r u LLLL ,� `m o 0 0 o mo mo mo 0 o 0 o u $Y. m C o� Toi 4a �$om$m e�J E a av a 3'E adz ( w d vz r I-I-HuuFUHH FF U 00Ov�0000 - aCG6 1 u at I'p o�000'E _ E N O O g O O$O O 9. 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W 3+ >>a o!+LLx ry ry rvrvrvry o. r v m�$moa0000 is ttt- Eo 000 °'mac IH o E C cs o' ' v E m ry ry N.. nom moy a -°„ 00...`*..N So o�V o Q o o ry.mJ o m cog 0 0 i,'°,> �LL000fo01 000 0a r ' ,. n..$000n�oN� E vi u"iu Na.m.ory vr.. 8 mz `-za 555�0rr,� LLx ' umi�m0o<0000a � �o�on°o�LLo�roufLLf�o 0000 oo o" 00i o o u l. 0c x n urvi a � d nB„ _ a Zm A N o = _ 1. _ = m = = 0 a o w w V_V _ =f3rvo Q�<< m a = dLL �N rN a a vLLa LL rLL ��LL LL �LL �= -=oLL „z° .�z a o" =oLL ,.z°��-z°O� i o=OLL ..z°r�«zoo eta : e. �E2Er o 'z ooz° \ w'u Er o 'z°uoz° u E` o •zLLozo f$LL0m n wz„zo a az°-,�z o o_ =E`e z;�z o_- `o E cF« u°..'LL E E H- _ ; „u«LL E E E US IN- = 3 LL E d E - - - 3 3o' v0EE „y ¢u Inc ry m o«LL �nm m in n o«LL ca4aa4n.0. cgagagQ,o,ry m" a o`v� Ed 6e.666 ddda Ed u udod Ena adn de „W`odZi .i 4 m e MDF Press Emissions Emission Description Annual Press Production Source ES-16 Scrubber controlling Press 272,230 MSF 3/4" ES-16 Scrubber controlling Press 6,145 hr r Scrubber Control Efficiencies VOC,Formaldehyde,and Methanol removal: 90% PM removal: 80% EF Uncontrolled Controlled Controlled Compound Reference Emission Factor Emissions,tpy Emissions,Ib/ r WPPIVOC 7.00E-02 Ib/MSF 0.00 0 PM 8.80E-02 Ib MSF 0.00 0 PM1O 8.80E-02 Ib MSF 0.00 0 PM2.5 8.80E-02 Ib MSF 0.00 0 Acetone 2.90E-02 Ib MSF 0.00 0 Acetone as propane .1D. 2.20E-02 Ib MSF 0.00 0 0 Acetaldehyde 75-07-0 TH) 3.50E-03 Ib MSF 0.00 0.0 Acrolein 107-02-8 TH 7.30E-04 Ib/MSF 0.000 0.0 Cumene `0 5.48E-05 Ib/MSF 0.0000 0.0 Formaldehyde 50-00-0 TH d 1.37E+00 Ib hr 0.00 0 O.o0E+00 Methanol 67-56-1 H o 2.12E+00 Ib hr 0.00 0 0 Methanol as propane 9.72E-01 Ib/MSF 0.00 0 Phenol 2.60E-02 Ib MSF 0.00 0 Pro ionaldeh de z° 5.40E-04 Ib/MSF O.D000 0.0 1.Source specific compliance testing November 2011 2.AP42,Section 10.6.3,Table 10.6.3-4. 3.Calculated Emission Factor 4.NCASI SARA 313 Guidance for Wood Products Facilities Updated March 2011 5.NCASI emission factor database cumene emissions from PB dry material dryer'1.5 ODT/MSF. Note. Stack testing was done in 2011 on the MDF press but the testing has not yet been accepted by the DAQ therefore,factors are not being used in the AEI. MDF Plant Dryer Scrubbers Emissions Emission Description Discharge Rate Operating Hours /Point NM, Hr SCFM Hrs Yr EP-02 Dryer Outfeed Scrubber No.1 116,000 73,544 7,191 EP44 Dryer Outfeed Scrubber No.2 116,000 73,544 NA Energy Plant Outlet 140,000 88,760 Annual Press Production: 272,230 MSF 3/4" Annual Press Production: 198,729 ODT/yr Ratio of MDF TO HDF 11.0%MDF Hog Fuel and Sanderdust combused in Teaford: 70,401,360 Ib/yr Green Wood Heating Value: 0.0087 MMBtu/lb 0.0087 Hog Fuel and Sanderdust combused in Teaford: 612,492 MMBtu/yr Total Firing Rate in Abort: 53,159 MMBtu/yr Teaford Firing Rate excluding Abort: 559,333 MMBtu/yr Energy system wood firing rate: 205 MMBtu/hr Energy System Natural Gas Use: 89.08 mmscf/yr 0.087331353 PM/metals control efficiency: 85% Soluble VOC control efficiency: 90% Emissions, Compound Emission Factor Reference Ib r Emissions,tpy PM from Combined Scrubber Outlet I 5.10E-01 Ib/ODT 13 101,351 50.68 PM10 assumes PM10=98%PM 5.10E-01 Ib/ODT 13 101,351 1 50.68 PM2.5 assumes PM2.5=PM10 5.10E-01 Ib/ODT 13 101,351 1 50.68 missions, Compound Uncontrolled Emission Factor Reference E "'on,, r Emissions,tpy WPPi VOC 3.27E+00 Ib/ODT 12 649,839 324.9 Methanol as propane 3.69E-02 Ib/ODT Calculated 734 0.4 Acetone not a VOC,HAP,or TAP 2.50E-02 Ib/ODT 6 497 0.2 Acetone as propane 1.90E-02 Ib/ODT Calculated 377 0.2 Cumene 3.39E-03 Ib/ODT 14 67 0.0 Formaldehyde 50-00-0TH MDF 1.58E+00 Ib/ODT 6 Formaldehyde 50-00-0TH HDF 1.18E+00 Ib/ODT 6 233,797 116.9 Acetaldehyde 75-07-0 TH .75E-02 Ib/ODT 6 348 0.2 Methanol 67-56-1 H MDF 7.08E-02 Ib/ODT 6 Methanol 67-56-1 H HDF 8.06E-02 Ib/ODT 6 15,803 7.9 Phenol 108-95-2 TH 8.60E-03 Ib/ODT 6 171 0.1 Compound Uncontrolled Emission Factor Reference Emissions, Emissions,tpy Refili ES-01 VOC as VOC 9.44E-01 Ib/ODT 9 0 0.00 WPPl VOC 1.10E+00 Ib/ODT 10 0 0.00 VOC as C 9.40E-01 Ib/ODT 8 0 0.00 VOC as propane 1.10E+00 Ib/ODT 8 0 0.00 Acetone not a VOC,HAP,or TAP 6.40E-03 Ib/ODT 8 0 0.00 Acetone as propane 4.86E-03 Ib/ODT Calculated 0 0.00 Methanol 67-56-1 H 7.30E-03 Ib/ODT 8 0 0.00 Methanol as propane 3.35E-03 Ib/ODT Calculated 0 0.00 Phenol 108-95-2 TH 4.50E-03 Ib/ODT 8 0 0.00 Compound Uncontrolled Emission Factor Reference Emibsions, Emissions,tpy @Wd Cooler ES-06{ WPPi VOC 1.49E-01 Ib/MSF 10 0 0.00 VOC as VOC 1.32E-01 Ib/MSF 9 0 0.00 VOC as C 7.70E-02 Ib/MSF 2 0 0.00 VOC as propane 9.41E-02 Ib/MSF Calculated 0 0.00 Acetone 9.20E-03 Ib/MSF 2 0 0.00 Acetone as propane 6.98E-03 Ib/MSF Calculated 0 0.00 Acetaldehyde 75-07-0TH 1.00E-03 Ib/MSF 2 0.00 0.00 Acrolein 107-02-8 TH 2.20E-04 Ib/MSF 2 0.00 0.00 Formaldehyde 50-00-0 TH 4.20E-02 JbIE 2 0.0 0.00 Methanol 67-56-1 H 2.50E-02 Ib/MSF 2 0.0 0.00 Methanol as propane I 1.15E-02 Ib/MSF Calculated 0.0 0.00 'Exhaust from the Refiners is routed through the dryers. 'Exhaust from the board cooler may be used as combustion air for the heat energy system or may be routed directly to the dryers. *Emissions are presented here for routing to dryers(higher than routing to energy system). MDF Plant Dryer Scrubbers Emissions Expected Emissions, Compound Uncontrolled Emission Factor Reference Scrubber ib/yr Emissions,tpy n I CO-at energy plant outlet flow 5.00E+01 m/Nm3 1 0 110,738 55.37 NOx-at energy plant outlet flow 3.30E-01 Ibs/MMBtu 13 0 184,580 92.29 SO2 2.50E-02 Ib/MMBtu 5 0 1.40E+04 6.99E+00 VOC 1.70E-02 Ib/MMBtu 5 below Acetaldehyde 75-07-0 TH 1.22E-04 Ib/MMBtu 3 0.9 6.82E+00 3.41E-03 Aceto henone 98-86-2 H 1.84E-06 Ib/MMBtu 3 0 1.03E+00 5.15E-04 Acrolein 107-02-8 TH 3.16E-05 Ib/MMBtu 3 0.9 1.77E+00 8.84E-04 Antimony&Compounds H 4.98E-07 Ib/MMBtu 4 0 2.79E-01 1.39E-04 Arsenic&Compounds TH 1.84E-06 Ib/MMBtu 4 0 1.03E+00 5.15E-04 Benzene 71-43-2 TH 2.35E-04 Ib/MMBtu 3 0 1.31E+02 6.57E-02 Benzo a rene 50-32-8 T 2.60E-06 Ib/MMBtu 5 0 1.45E+00 7.27E-04 Beryllium T/H 3.41E-07 Ib/MMBtu 4 0 1.91E-01 9.54E-05 Cadmium T/H 1.85E-06 Ib/MMBtu 4 0 1.03E+00 5.17E-04 Carbon tetrachloride 56-23-5 TH 1.26E-05 Ib/MMBtu 3 0 7.05E+00 3.52E-03 Chlorine 7782-50-5 TH 7.90E-04 Ib/MMBtu 5 0.85 6.63E+01 3.31E-02 Chlorobenzene 108-90-7 TH 1.66E-05 Ib/MMBtu 3 0 9.28E+00 4.64E-03 Chloroform 67-66-3 TH 3.52E-05 Ib/MMBtu 3 0 1.97E+01 9.84E-03 Chromium H 5.06E-06 Ib/MMBtu 4 0 2.83E+00 1.42E-03 Chromium VI T/H 2.35E-07 Ib/MMBtu 4 0 1.31E-01 6.57E-05 Cobalt compounds H 1.97E-07 Ib/MMBtu 4 0 1.10E-01 5.51E-05 Dinitro henol,2,4- 51-28-5 H 1.30E-07 Ib/MMBtu 3 0 7.27E-02 3.64E-05 D E H P 117-81-7 TH 4.70E-08 Ib/MMBtu 5 0 2.63E-02 1.31E-05 Ethyl benzene 100-41-4 H 1.76E-05 Ib/MMBtu 3 0 9.84E+00 4.92E-03 Ethylene dichloride 107-06-2 TH 2.90E-05 Ib/MMBtu 5 0 1.62E+01 8.11E-03 Formaldehyde 50-00-0 TH 8.83E-04 Ib/MMBtu 3 below 1,2,3,6,7,8-HCDD T 1.60E-06 Ib/MMBtu 5 0 8.95E-01 4.47E-04 Hydrogen chloride 7647-01-0 TH 1.57E-03 Ib/MMBtu 3 0.85 1.32E+02 6.59E-02 Lead and Lead compounds H 1.66E-05 Ib/MMBtu 4 0 9.28E+00 4.64E-03 Manganese&compounds TH 2.62E-05 Ib/MMBtu 4 0 1.47E+01 7.33E-03 MercuryT/H 6.61E-07 Ib/MMBtu 4 0 3.70E-01 1.85E-04 Methanol 4.87E-04 Ib/MMBtu 3 0.9 2.72E+01 1.36E-02 Methyl bromide 74-83-9 H bromomethane 1.52E-05 Ib/MMBtu 3 0 8.50E+00 4.25E-03 Methyl chloride 74-87-3 H chloromethane 2.31E-05 Ib/MMBtu 3 0 1.29E+01 6.46E-03 Methyl chloroform 71-55-6TH 3.10E-05 Ib/MMBtuFE 0 1.73E+01 8.67E-03 Methyl eth lketone 78-93-3 T 5.39E-06 Ib/MMBtu0.9 3.01E-OS 1.51E-04 Meth lene chloride 75-09-2 TH 3.50E-04 Ib/MMBtu0 1.96E+02 9.79E-02 Na hthalene 91-20-3 H 7.44E-05 Ib/MMBtu0 4.16E+01 2.08E-02 Nickel T/H 3.94E-06 Ib/MMBtu0 2.20E+00 1.10E-03 Nitro henol,4- 100-02-7 H 9.32E-08 Ib/MMBtu0 5.21E-02 2.61E-05 Pentachloro henol 87-86-5 TH 4.48E-08 Ib/MMBtu0 2.51E-02 1.25E-05 Perchloroeth lene 127-18-4 TH 3.80E-05 Ib/MMBtu0 2.13E+01 1.06E-02 Phenol 108-95-2 TH 1.98E-05 Ib/MMBtu0.9 1.11E+00 5.54E-04 Phos horus 7723-14-0 H 9.85E-OS Ib/MMBtu4 0 5.51E+01 2.75E-02 Polychlorinated bi hen Is 1336-36-3 TH 8.15E-09 Ib/MMBtu 5 0 4.56E-03 2.28E-06 Pol c clic Organic Matter H 1.25E-04 Ib/MMBtu 5 0 6.99E+01 3.50E-02 Pro ionaldeh de 123-38-6 H 3.21E-05 Ib/MMBtu 3 0.9 1.80E+00 8.98E-04 Propylene dichloride 78-87-5 H 3.30E-05 Ib/MMBtu 5 0 1.85E+01 9.23E-03 Selenium compounds H 1.85E-06 Ib/MMBtu 4 0 1.03E+00 5.17E-04 Styrene 100-42-5 TH 6.30E-05 Ib/MMBtu 3 0 3.52E+01 1.76E-02 2,3,7,8-TCDD 1746-01-6TH 8.60E-12 Ib/MMBtu 5 0 4.81E-06 2.41E-09 Toluene 108-88-3 TH 2.34E-05 Ib/MMBtu 3 0 1.31E+01 6.54E-03 Trichloroeth lene 79-01-6TH 1.94E-05 Ib/MMBtu 3 0 1.09E+01 5.43E-03 Trichlorofluoromethane 75-69-4T 4.05E-05 Ib/MMBtu 3 0 2.27E+01 1.13E-02 Trichloro henol,2,4,6- 88-06-2 H) 2.73E-07 Ib/MMBtu 3 0 1.53E-01 7.63E-05 Vin (chloride 75-01-4 TH 1.84E-05 Ib/MMBtu 3 0 1.03E+01 5.15E-03 X lene 1330-20-7 TH 5.22E-06 Ib/MMBtu 3 0 2.92E+00 1.46E-03 'Wood is burned in the energy plant and the hot exhaust is routed to the dryers. Natural gas maybe burned as auxiliary/startup/standby fuel.Dryer exhaust is routed to 2 wet scrubbers in parallel. Compound Emission Factor Reference lb r Emissions, Emissions,tpy FS02t a"jS40ft- NOx 5.00E+01 Ib/mmscf 11 4.45E+03 2.23E+00 CO 8.40E+01 Ib/mmscf 11 7.48E+03 3.74E+00 PM/PM10/PM2.5 7.60E+00 Ib/mmscf 11 6.77E+02 3.38E-01 SO2 6.00E-01 Ib/mmscf 11 5.34E+01 2.67E-02 VOC 5.50E+00 Ib/mmscf 11 4.90E+01 2.45E-02 Benzene 71-43-2 TH 2.10E-03 Ib/mmscf 11 1.87E-01 9.35E-05 Benzo a rene 50-32-8 T 1.20E-06 Ib/mmscf 11 1.07E-04 5.34E-08 Cobalt compounds H 8.40E-05 Ib/mmscf 11 1.12E-03 5.61E-07 Formaldehyde 50-00-0 TH 7.50E-02 Ib/mmscf 11 6.68E-01 3.34E-04 Hexane 1.80E+00 Ib/mmscf 1.60E+02 8.02E-02 Naphthalene 91-20-3 H 6.10E-04 Ib/mmscf 11 5.43E-02 2.72E-05 Selenium com ounds H 2.40E-05 Ib/mmscf 11 3.21E-04 1.60E-07 Toluene 108-88-3 TH 3.40E-03 Ib/mmscf 11 3.03E-01 1.51E-04 Ref: 1.Emission Factors based on Manufacturer data. 2.AP-42,Table 10.6.3-6,2002 3.Emission factors from NCASI TB 973,Table 7.1-Uncontrolled,February 2010 4.Emission factors from NCASI TB 973,Table7.2 Controlled:Wet Scrubber,February 2010 S.Emission factors from AP-42-DAQ spreadsheet 6.Emission factors per NCASI TB770,Table 6.1.2 Mill 132 average.January 1999 7.Emission factors from NCASI TB 770,Table 6.4.2,Mill 142 No.1 Board Cooler,January 1999 B.Emission Factors AP-42 9.VOC as VOC=VOC as C+formaldehyde+0.5 methanol 10.WPPi VOC=VOC as propane+methanol+formaldehyde-0.65•methanol as propane-0.65'acetone as propane 11.Emission factors based on AP-42,Fifth Edition,Chapter 1,Section 4.Taken from DAQ spreadsheet online.July 1998 12.Source specific testing on November 2011. 13.Source specific testing on November 2014. MDF Plant Dryer Scrubbers Emissions 14.NCASI emission factor database cumene emissions from fiberboard refiner wet wood(50%moisture) MDF Teaford Abort Wood Burned during Abort: 53,159 MMBtu/yr Annual Press Production: 198,728 CDT/yr Compound Uncontrolled Emission Factor Reference Emissions, Emissions,tpy N PM Total 5.60E-01 lb/MMBtu (4) 2.98E+04 1.49E+01 PM10 5.00E-01 lb/MMBtu (4) 2.66E+04 1.33E+01 PM2.5 4.30E-01 lb/MMBtu 4 2.29E+04 1.14E+01 CO 6.00E-01 lb/MMBtu (4) 3.19E+04 1.59E+01 NOx 3.30E-01 lb/MMBtu (6) 1.75E+04 8.77E+00 SO2 2.50E-02 lb/MMBtu (4) 1.33E+03 6.64E-01 VOC 1.70E-02 lb/MMBtu (4) 9.04E+02 4.52E-01 Acetaldeh de(75-07-0TH) 1.22E-04 Ib/MMBtu (2) 6.49E+00 3.24E-03 Aceto henone 98-86-2 H) 1.84E-06 lb/MMBtu 2 9.78E-02 4.89E-05 Acrolein 107-02-8TH) 3.16E-05 lb/MMBtu 2 1.68E+00 8.40E-04 Antimon &Compounds H 4.98E-07 lb/MMBtu 3 2.65E-02 1.32E-05 Arsenic&Compounds (TH) 1.84E-06 lb/MMBtu (3) 9.78E-02 4.89E-05 Benzene(71-43-2 TH) 2.35E-04 lb/MMBtu 2 1.25E+01 6.25E-03 Benzo(a) rene (50-32-8T) 2.60E-06 lb/MMBtu (4) 1.38E-01 6.91E-05 Beryllium T/H 3.41E-07 lb/MMBtu (3) 1.81E-02 9.06E-06 Cadmium T/H 1.85E-06 lb/MMBtu (3) 9.83E-02 4.92E-05 Carbon tetrachloride(56-23-5 TH) 1.26E-05 lb/MMBtu 2) 6.70E-01 3.35E-04 Chlorine(7782-50-5 TH) 7.90E-04 lb/MMBtu (4) 4.20E+01 2.10E-02 Chlorobenzene(108-90-7 TH) 1.66E-05 lb/MMBtu 2 8.82E-01 4.41E-04 Chloroform 67-66-3 TH) 3.52E-05 lb/MMBtu (2) 1.87E+00 9.36E-04 Chromium(H) 5.06E-06 lb/MMBtu 3) 2.69E-01 1.34E-04 Chromium(VI)(T/H) 2.35E-07 lb/MMBtu (3) 1.25E-02 6.25E-06 Cobalt compounds(H) 1.97E-07 lb/MMBtu 3 1.05E-02 5.24E-06 Dinitro henol,2,4-(51-28-5 H) 1.30E-07 lb/MMBtu (2) 6.91E-03 3.46E-06 DEHP(117-81-7 TH) 4.70E-08 lb/MMBtu (4) 2.50E-03 1.25E-06 Ethyl benzene 100-41-4 H) 1.76E-05 lb/MMBtu 2 9.36E-01 4.68E-04 Ethylene dichloride(107-06-2 TH) 2.90E-05 lb/MMBtu (4) 1.54E+00 7.71E-04 Formaldehyde(50-00-0 TH) 8.83E-04 lb/MMBtu 2 4.69E+01 2.35E-02 1,2,3,6,7,8-HCDD(T) 1.60E-06 lb/MMBtu (4) 8.51E-02 4.25E-05 Hydrogen chloride(7647-01-0TH) 1.57E-03 lb/MMBtu (2) 8.35E+01 4.17E-02 Lead and Lead compounds(H) 1.66E-05 lb/MMBtu 3) 8.82E-01 4.41E-04 Manganese&compounds(TH) 2.62E-05 lb/MMBtu (3) 1.39E+00 6.96E-04 Mercury(T/H) 6.61E-07 lb/MMBtu (3) 3.51E-02 1.76E-05 Methanol 4.87E-04 lb/MMBtu (2) 2.59E+01 1.29E-02 Methyl bromide(74-83-9 H)(bromomethane) 1.52E-05 lb/MMBtu (2) 8.08E-01 4.04E-04 Methyl chloride(74-87-3 H)(chloromethane) 2.31E-05 lb/MMBtu (2) 1.23E+00 6.14E-04 Methyl chloroform(71-55-6 TH) 3.10E-05 lb/MMBtu 4 1.65E+00 8.24E-04 Methyl ethyl ketone(78-93-3 T) 5.39E-06 lb/MMBtu (2) 2.87E-01 1.43E-04 Methylene chloride(75-09-2 TH) 3.50E-04 lb/MMBtu (2) 1.86E+01 9.30E-03 Naphthalene 91-20-3 H) 7.44E-05 lb/MMBtu (2) 3.96E+00 1.98E-03 Nickel (T/H) 3.94E-06 lb/MMBtu (3) 2.09E-01 1.05E-04 Nitro henol,4-(100-02-7 H) 9.32E-08 lb/MMBtu (2) 4.95E-03 2.48E-06 Pentachloro henol(87-86-5 TH) 4.48E-08 lb/MMBtu 2 2.38E-03 1.19E-06 Perch loroeth lene(127-18-4 TH) 3.80E-05 lb/MMBtu 4 2.02E+00 1.01E-03 Phenol(108-95-2 TH) 1.98E-05 lb/MMBtu (2) 1.05E+00 5.26E-04 Phosphorus(7723-14-0 H) 9.85E-05 lb/MMBtu (3) 5.24E+00 2.62E-03 Polychlorinated bi hen Is (1336-36-3TH) 8.15E-09 lb/MMBtu (4) 4.33E-04 2.17E-07 Polycyclic Organic Matter (H) 1.25E-04 lb/MMBtu (4) 6.64E+00 3.32E-03 Pro ionaldeh de(123-38-6 H) 3.21E-05 lb/MMBtu 2) 1.71E+00 8.53E-04 Propylene dichloride(78-87-5 H) 3.30E-05 lb/MMBtu (4) 1.75E+00 8.77E-04 Selenium compounds H) 1.85E-06 lb/MMBtu (3) 9.83E-02 4.92E-05 Styrene 100-42-5 TH) 6.30E-05 lb/MMBtu (2) 3.35E+00 1.67E-03 2,3,7,8-TCDD 1746-01-6 TH 8.60E-12 lb/MMBtu (4) 4.57E-07 2.29E-10 Toluene 108-88-3 TH) 2.34E-05 lb/MMBtu (2) 1.24E+00 6.22E-04 Trichloroeth lene(79-01-6 TH) 1.94E-05 lb/MMBtu 2) 1.03E+00 5.16E-04 Trichlorofluoromethane(75-69-4 T) 4.05E-05 lb/MMBtu (2) 2.15E+00 1.08E-03 Trichloro henol,2,4,6-(88-06-2 H) 2.73E-07 lb/MMBtu (2) 1.45E-02 7.26E-06 Vin (chloride(75-01-4TH) 1.84E-05 lb/MMBtu (2) 9.78E-01 4.89E-04 X lene 1330-20-7TH) 5.22E-06 lb/MMBtu (2) 2.77E-01 1.39E-04 "Wood is burned in the energy plant and the hot exhaust is routed to the dryers. Natural gas may be burned as auxiliary/startup/standby fuel. Dryer exhaust is routed to 2 wet scrubbers in parallel. Notes: 1.Emission Factors based on Manufacturer data. 2.Emission factors from NCASI TB 973,Table 7.1-Uncontrolled,February 2010 3.Emission factors from NCASI TB 973,Table7.2 Controlled:Wet Scrubber,February 2010 4.Emission factors from AP-42-DAQ spreadsheet 5.Firing rate based on tracking data,20-25 MMBtu and using 25 MMBtu as a conservative estimate. 6.Source specific testing in November 2014. MDF Plant Emissions for Backup Natural Gas Burners for Thermal Oil Heater(ES-18,-19,40) If the wood energy system is offline and the MDF process is still running,backup natural gas burners can be used to provide heat to the thermal oil system. These burners will have their own emission points,EP-18,-19,-20. #of Burners: 3 Burner Size: 24 MMbtu/hr Natural Gas Heating Value: 1020 BTU/scf Burner Natural Gas Use: 67.16 MMscf/yr Each-for AERO Compound Emission Factor I'I Emissions Emissions Emissions Emissions Ib/ r tpY Ib/ r tpY PM 7.60E+00 Ib/MMscf 5.10E+02 2.55E-01 PM 1.70E+02 0.09 PM10 7.60E+00 lb/MMscf 5.10E+02 2.55E-01 PM10 1.70E+02 0.09 PM2.5 7.60E+00 Ib/MMscf 5.10E+02 2.55E-01 PM2.5 1.70E+02 0.09 S02 6.00E-01 Ib/MMscf 4.03E+01 2.01E-02 502 1.34E+01 0.01 NOx 1.00E+02 Ib/MMscf 6.72E+03 3.36E+00 NOx 2.24E+03 1.12 CO 8.40E+01 Ib/MMscf I 5.64E+03 2.82E+00 CO 1.88E+03 0.94 VOC 5.50E+00 Ib/MMscf 3.69E+02 1.85E-01 VOC 1.23E+021 0.06 Arsenic 2.00E-04 Ib/MMscf 1.34E-02 6.72E-06 Arsenic 4.48E-03 2.24E-06 Barium 4.40E-03 Ib/MMscf 2.95E-01 1.48E-04 Barium 9.85E-02 4.92E-05 Benzene 2.10E-03 Ib/MMscf 1.41E-01 7.05E-05 Benzene 4.70E-02 2.35E-05 Cadmium 1.10E-03 Ib/MMscf 7.39E-02 3.69E-05 Cadmium 2.46E-02 1.23E-05 Chromium 1.40E-04 Ib/MMscf 9.40E-03 4.70E-06 Chromium 3.13E-03 1.57E-06 Cobalt 8.40E-05 Ib/MMscf 5.64E-03 2.82E-06 Cobalt 1.88E-03 9.40E-07 Formaldehyde 7.50E-02 Ib/MMscf 5.04E+00 2.52E-03 Formaldehyde 1.68E+00 8.39E-04 Lead 5.00E-04 Ib/MMscf 3.36E-02 1.68E-05 Lead 1.12E-02 5.60E-06 Manganese 3.80E-04 Ib/MMscf 2.55E-02 1.28E-05 Manganese 8.51E-03 4.25E-06 Mercury 2.60E-04 Ib/MMscf 1.75E-02 8.73E-06 Mercury 5.82E-03 2.91E-06 Naphthalene 6.10E-04 Ib/MMscf 4.10E-02 2.05E-05 Naphthalene 1.37E-02 6.83E-06 Nickel 2.10E-03 Ib/MMscf 1.41E-01 7.05E-05 Nickel 4.70E-02 2.35E-05 Toluene 3.40E-03 Ib/MMscf 2.28E-01 1.14E-04 Toluene 7.61E-02 3.81E-05 1.AP-42 Section 1.4.July 1998 MDF Backup Generator Emissions(ES-21) Generator Usage: 27 hrs/yr Generator HP Rating 1592 hp Annual Output 42984 hp-hr Emission Compound Factor"I Actual Emissions Ib/hp-hr Ib/yr tpy PM 7.00E-04 3.01E+01 1.50E-02 PM10 7.00E-04 3.01E+01 1.50E-02 PM2.5 7.00E-04 3.01E+01 1.50E-02 502 4.05E-03 1.74E+02 8.69E-02 NOx 2.40E-02 1.03E+03 5.16E-01 VOC 7.05E-04 3.03E+01 1.52E-02 CO 5.50E-03 2.36E+02 1.18E-01 Acetaldehyde 1.76E-07 7.58E-03 3.79E-06 Acrolein 5.52E-08 2.37E-03 1.19E-06 Arsenic unlisted compounds 2.80E-08 1.20E-03 6.02E-07 Benzene 5.43E-06 2.33E-01 1.17E-04 Benzo(a)pyrene 1.80E-09 7.73E-05 3.87E-08 Beryllium metal(unreacted) 2.10E-08 9.03E-04 4.51E-07 Cadmium metal(elemental unreacted) 2.10E-08 9.03E-04 4.51E-07 Chromic Acid(VI) 2.10E-08 9.03E-04 4.51E-07 Formaldehyde 5.52E-07 2.37E-02 1.19E-05 Lead unlisted compounds 6.30E-08 2.71E-03 1.35E-06 MDF Plant Fugitive Emissions: Resin Tanks(MDFR-1,MDFR-2,MDFR-3) Number of Resin Tanks: 3 resin tanks Uncontrolled Emission Fugitive Emissions, Fugitive Compound Factor Ib/yr Emissions,tpy UIF Resin Tanks VOC 0.001lb/hr/tank 26.4 1.32E-02 Formaldehyde(50-00-0 TH) 0.001 Ib/hr/tank 26.4 1.32E-02 Methanol(50-00-0 TH) 0.01 Ib/hr/tank 263.5 1.32E-01 1.Emission Factor based on PCWP Rule Table 2A PB Plant Press(DEF-2030)and Board Cooler(PB-BC)Emissions 2015 Press Abort Gate Hrs: 27 Hrs. 2015 Press Production: 115,372 MSF(0.75")/year Emission Actual Emissions EF Compound Factor Ib/MSF Ibs/hr Ibs/ r t Reference Partideboard Press PM 3.39E+00 92 0.05 (2) PM-10 3.39E+00 92 0.05 (2) PM-2.5 1.17E+00 32 0.02 (2) NOx 3.97E-01 11 0.01 (2) VOC asC 2.12E+01 572 0.29 (2) VOC asPropane 2.59E+01 699 0.35 1 (2) VOC asVOC 4.06E+01 1,097 0.55 (3) CO 4.00E-02 1 0.00 (2) Acetaldehyde 1.40E-02 1.68E-01 0 0.00 (2) Acrolein 1.70E-03 1.81E-02 0 0.00 (2) Cumene 5.48E-05 0.00 0.00000 (2) Formaldehyde 2.30E-01 6.47E+00 6 0.00 (2) Methanol 5.20E-01 1.65E+01 14 0.01 (2) Methyl Ethyl Ketone I 9.30E-04 I 1 0 1 0.00001 1 (1) Phenol 1.98E-01 0.00 0.00000 (2) Pro ionaldeh de 9.90E-03 0.00 0.00000 (2) 1. NCASI TB 771,Table 6.3.1,January 1999 2. December 21,2005 Stack Testing. Assume PM10=PM,and assume PM2.5=condensible PM. 3. VOC as VOC=VOC as Propane+Formaldehyde+0.5*Methanol 4.NCASI emission factor database cumene emissions from PB dry material dryer*1.5 ODT/MSF. Note:press was capped and source emissions taken into the PB dryers and dryer controls on 10/31/11. 2015 Board Cooler Production: 115,372 MSF(0.75")/year Emission Actual Emissions EF Compound Factor Reference Ib/MSF Ibs/ r tpY Board Cooler PM 2.27E-01 26190 13.09 (2) PM-10 2.27E-01 26190 13.09 (2,3) PM-2.5 7.70E-02 8884 4.44 (2,3) VOC asC 7.20E-02 8307 4.15 (1) VOC asPropane 8.80E-02 10153 5.08 Calculated VOC as VOC 1.42E-01 1 16383 8.19 1 (5) CO 1.50E-01 17306 8.65 (2) Acetaldehyde 1.30E-03 150 0.07 (4) Acrolein 3.60E-04 42 0.02 (4) Cumene 5.48E-05 6 0.003 (4) Formaldehyde 2.70E-02 3115 1.56 (4) Methanol 5.40E-02 6230 3.12 (4) Methyl Ethyl Ketone I 1.10E-04 1 13 1 0.01 1 (2) Phenol I 4.70E-03 1 542 1 0.27 1 (4) 1. Emission Factors from TB771,6.4.1,Board Cooler Average Emissions,January 1999 2. AP-42 Wood Products Industry-Particleboard Manufacturing,10.6.2 June 2002. 3. Assume PM10=PM,and assume PM2.5=condensible PM. 4. NCASI SARA 313 Guidance Updated 2011-Median Values 5. VOC as VOC=VOC as Propane+Formaldehyde+0.5*Methanol PS Plant Wellons Bypass Emissions • 40 MMBtu/hr 8,000 Btu/Ib dry basis Calculated Firing Rate: 2.5 ton/hr Wellons Gas Consumed: 142.0 MMscf Wellons Bypass Hours: 12.0 hr/yr Heating Value of Green Wood: 0.0087 MMBtu/lb Bypass Wood Combusted: 60,000 Ib/yr Bypass Wood Combustion: 522 MMStu/yr Compound Emission Factor Emission Factor Actual Emission EF Units Reference Ib/MMBtu Ibs/r tpy PM 5.60E-01 Ib/MMBtu 2.92E+02 1.46E-01 (3) PM-10 5.00E-01 Ib/MMBtu 2.61E+02 1.31E-01 (3) PM-2.5 4.30E-01 Ib/MMBtu 2.24E+02 1.12E-01 (3) VOC 1.70E-02 Ib/MMBtu 8.87E+00 4.44E-03 (3) NOx 2.20E-01 Ib/MMBtu 1.15E+02 5.74E-02 (3) sox 2.50E-02 Ib/MMBtu 1.31E-01 6.53E-03 (3) CO 6.00E-01 Ib MMBtu 3.13E+02 1.57E-01 3 Acetaldehyde 1.22E-04 Ib/MMBtu 6.37E-02 3.18E-05 (1) Acrolein 3.16E-05 Ib/MMBtu 1.65E-02 8.25E-06 (1) Antimony 4.23E-07 Ib/MMBtu 2.21E-04 1.10E-07 (4) Arsenic 3.02E-06 Ib/MMBtu 1.58E-03 7.88E-07 (2) Benzene 2.35E-04 Ib/MMBtu 1.23E-01 6.13E-05 (1) Benzo(a)pyrene 2.60E-06 Ib/MMBtu 1.36E-03 6.79E-07 (3) Beryllium 4.27E-05 Ib/MMBtu 2.23E-02 1.11E-05 (2) Cadmium 4.67E-06 Ib/MMBtu 2.44E-03 1.22E06 (2) Chlorine 7.90E-04 Ib/MMBtu 4.12E-01 2.06E-04 (3) Chlorobenze 1.66E-05 Ib/MMBtu 8.67E-03 4.33E-06 (1) Chloroform 3.52E-05 Ib/MMBtu 1.84E-02 9.19E-06 (1) Chromium 3.46E-05 Ib/MMBtu 1.81E-02 9.03E-06 (2) Chromium VI 6.97E-06 Ib/MMBtu 3.64E-03 1.82E-06 (2) Cobalt 1.96E-05 Ib/MMBtu 1.02E-02 5.12E-06 (2) Ethylbenzene 1.76E-05 Ib/MMBtu 9.19E-03 4.59E-06 (1) Formaldehyde 8.83E-04 Ib/MMBtu 4.61E-01 2.30E-04 (1) HCI 1.57E-03 Ib/MMBtu 8.20E-01 4.10E-04 (1) Lead 1.77E-05 Ib/MMBtu 9.24E-03 4.62E-06 (2) Manganese 1.81E-03 Ib/MMBtu 9.45E-01 4.72E-04 (2) MEK 5.39E-06 Ib/MMBtu 2.81E-03 1.41E-06 (1) Mercury 5.00E-07 Ib/MMBtu 2.61E-04 1.31E-07 (2) Naphthalene 7.44E-05 Ib/MMBtu 3.88E-02 1.94E-05 (1) Nickel 2.26E-05 Ib/MMBtu 1.18E-02 5.90E-06 (2) Phenol 1.98E-05 Ib/MMBtu 1.03E-02 5.17E-06 (1) POM 1.06E-04 ib/MMBtu 5.53E-02 2.76E-05 (1),(3) Selenium 2.53E-06 Ib/MMBtu 1.32E-03 6.60E-07 (2) Trichlorofluoromethane 4.05E-05 Ib/MMBtu 2.11E-02 1.06E-05 (1) Styrene 6.30E-05 Ib/MMBtu 3.29E-02 1.64E-05 (1) Toluene 2.34E-05 Ib/MMBtu 1.22E-02 6.11E-06 (I) )(lene 5.22E-06 Ib MMBtu 2.72E-03 1.36E-06 1 RYid Compound Emission Factor is) Emissions Emissions Ib/r tpy PM 7.60E+00 Ib/MMscf 1.08E+03 5.39E-01 PM10 7.60E+00 Ib/MMscf 1.08E+03 5.39E-01 PM2.5 7.60E+00 Ib MMscf 1.08E+03 5.39E-01 S02 6.00E-01 Ib MMscf 8.52E-01 4.26E-02 NOx 1.00E+02 Ib MMscf 1.42E+04 7.10E+00 CO 8.40E+01 Ib MMscf 1.19E+04 5.96E+00 VOC 5.50E+00 Ib MMscf 7.81E+02 3.90E-01 Arsenic 2.00E-04 Ib MMscf 2.84E-02 1.42E-05 Barium 4.40E-03 Ib MMscf 6.25E-01 3.12E-04 Benzene 2.10E-03 Ib MMscf 2.98E-01 1.49E-04 Cadmium 1.10E-03 Ib MMscf 1.56E-01 7.81E-05 Chromium 1.40E-04 Ib/MMscf 1.99E-02 9.94E-06 Cobalt 8.40E-05 Ib/MMscf 1.19E-02 5.96E-06 Formaldehyde 7.50E-02 Ib MMscf 1.06E+01 5.32E-03 Lead 5.00E-04 Ib/MMscf 7.10E-02 3.55E-05 Manganese 3.80E-04 Ib MMscf 5.39E-02 2.70E-05 Mercury 2.60E-04 Ib/MMscf 3.69E-02 1.85E-05 Naphthalene 6.10E-04 Ib/MMscf 8.66E-02 4.33E-05 Nickel 2.10E-03 Ib MMscf 2.98E-01 1.49E-04 Toluene 3.40E-03 Ib MMscf 4.83E-01 I 2.41E-04 1.NCASI TB 973,Table 7.1-Uncontrolled,February 2010 2.NCASI TB 973,Table 7.2-Control:Mechanical Collector,February 2010 3.AP-42 Section 1.6-wood residue combustion in boilers. 4.NCASI TB 973,Table 7.2-Control:Fabric Filter,February 2010 Wellons contributes 24 MMBtu/hr to Core Layer Dryer(74 MMBtu/hr total,normal operation) and contributes 16 MMBtu/hr to Surface Layer Dryer(56 MMBtu/hr total,normal operation) Beginning July 2007 exhaust from this source goes through the PB dryers and Wet ESP.However,during startup,the exhaust is bypassed to atmosphere. As designed,this bypass occurs for 0.25-0.5 hour prior to dryers being started.The emissions are counted in the dryers exhaust except startup. Startup emissions are accounted for in this calculation. 5.AP-42 Section 1.4.July 1998 • PB Plant Particleboard Dryer Emissions(1430,1420,1410,3201) 2 Core Layer Dryers,1 Surface Layer Dryer,and 1 Wellons Dryer Production: 115,372 MSF(3/4"inch)/yr PB Board Density: 44.5 Ib/ft' Dryer Production: 144,396 CDT/yr Dryer Operation Hours: 4,805 hr/yr Heating Value of Green Wood: 0.0087 MMBtu/Ib Hog Fuel and Sanderdust Combustion: 60,469,794 Ib/yr Natural Gas Usage(backup) 16.51 MMSCF/yr Hog Fuel and Sanderdust Combustion: 526,087.21 MMBtu/yr Natural Gas Heating Value: 1020 Btu/scf Total Dryer Heat Input: 160 MMBtu/hr Natural Gas Usage(backup) 105.2 hours Natural Gas (backup) WESP Wood Natural Gas Total Total Compound Wood Emission Factor Emission Factor REF Emission Factor Control Combustion Combustion Emissions Emissions Units P1 Emissions Emissions Ib/MMscf % Ib/yr Ib/yr Ib/yr Tons/yr PM filterable total) 2.35E+00 Ib/hr (3) 1.10E+04 O.00E+00 1.10E+04 5.52E+00 PM(condensible,total) 6.54E+00 Ib/hr (3) 3.07E+04 0.00E+00 3.07E+04 1.54E+01 PM total 8.89E+00 Ib/hr 3 7.6 4.18E+04 1.25E+02 4.19E+04 2.10E+01 PM10 filterable total 2.35E+00 Ib/hr 3 1.10E+04 O.ODE+00 1.10E+04 5.52E+00 PM10 condensible,total 6.54E+00 Ib/hr 3 3.07E+04 O.COE+00 3.07E+D4 1.54E+01 PM10 total 00I 8.89E+00 Ib/hr (3) 7.6 4.18E+04 1.25E+02 4.19E+04 2.10E+01 PM2.5 filterable total 2.02E+00 Ib/hr (3),(13) 9.50E+03 O.00E+00 9.50E+03 4.75E+00 PM2.5 icondensible,total 6.54E+00 Ib/hr 3 3.07E+04 0.00E+00 3.07E+04 1.54E+01 PM2.5 total 8.56E+00 Ib/hr (3),(13) 4.02E+04 O.00E+00 4.02E+04 2.01E+01 VOC as C I'I 4.03E+01 Ib/hr (3) 1.89E+05 O.00E+00 1.89E+05 9.47E+01 VOC as propane 4.93E+01 Ib/hr Calculated 2.31E+05 0.00E+00 2.31E+05 1.16E+02 VOC as VOC I'I 5.31E+01 Ib/hr (2),(3) 5.5 2.49E+05 9.08E+01 2.50E+OS 1.25E+02 WPPI VOC 5.37E+01 Ib/hr (12) 2.52E+05 O.00E+00 2.52E+OS 1.26E+02 NOx 5.67E+01 Ib/hr (3) 50 2.66E+05 8.25E+02 2.67E+05 1.34E+02 CO 1.26E+02 Ib/hr (3) 84 5.91E+05 1.39E+03 5.92E+05 2.96E+02 Sox 2.50E-02 Ib/MMBtu (7) 0.6 13152.18021 9.90E+00 1.32E+04 6.58E+00 Acetaldehyde 1.06E+00 Ib/hr 2 4.98E+03 O.DOE+00 4.98E+03 2.49E+00 Acetone 1.62E-04 Ib/MMBtu (4) 8.52E+01 O.00E+00 8.52E+01 4.26E-02 Acetone as propane 1.97E-02 Ib/hr (11) 9.24E+01 O.DOE+00 9.24E+01 4.62E-02 Acrolein 3.25E-01 Ib/hr (2) 1.53E+03 0.00E+00 1.53E+03 7.64E-01 Arsenic 3.21E-07 Ib/MMBtu (5) 1.69E-01 O.00E+00 1.69E-01 8.44E-05 Benzene 2.35E-04 Ib/MMBtu (4) 2.10E-03 1.24E+02 3.47E-02 1.24E+02 6.18E-02 Benzo a rene 2.60E-06 Ib/MMBtu (7) 1.20E-06 45% 7.52E-01 1.09E-05 7.52E-01 3.76E-04 Bromine 2.44E-05 Ib/MMBtu (7) 1.28E+01 O.DOE+00 1.28E+01 6.41E-03 Cadmium 3.73E-07 Ib/MMBtu (5) 1.96E-01 O.DOE+00 1.96E-01 9.81E-05 Chlorine 7.90E-04 Ib/MMBtu (7) 4.16E+02 0.00E+00 4.16E+02 2.08E-01 Chloroform 2.80E-05 Ib/MMBtu (7) 1.47E+01 O.00E+00 1.47E+01 7.37E-03 Chromium 8.04E-07 Ib/MMBtu (5) 4.23E-01 0.00E+00 4.23E-01 2.11E-04 Chromium VI 2.72E-07 Ib/MMBtu (5) 1.43E-01 O.00E+00 1.43E-01 7.15E-05 Cobalt 4.68E-07 Ib/MMBtu (5) 8.40E-05 2.46E-01 1.39E-03 2.48E-01 1.24E-04 Cumene 3.39E-03 Ib/CDT (14) 4.90E+02 0.00E+00 4.90E+02 2.45E-01 Formaldehyde 2.24E+00 Ib/hr (2) 7.50E-02 1.05E+04 1.24E+00 1.05E+04 5.26E+00 HCI 1.57E-03 Ib/MMBtu (4) 8.26E+02 O.o0E+00 8.26E+02 4.13E-01 Lead 4.95E-06 Ib/MMBtu (5) 2.60E+DO O.00E+00 2.60E+00 1.30E-03 Manganese 3.50E-05 Ib/MMBtu (5) 1.84E+01 O.o0E+00 1.84E+01 9.21E-03 Methanol 3.17E+00 Ib/hr (2) 1.49E+04 O.o0E+00 1.49E+04 7.45E+00 Methanol as propane 1.45E+00 Ib/hr 11 6.83E+03 O.00E+00 6.83E+03 3.41E+00 M E K 9.60E-03 Ib/ODT 6 1.39E+03 O.00E+00 1.39E+03 6.93E-01 Mercury 4.02E-07 Ib/MMBtu (5) 2.11E-01 0.00E+00 2.11E-01 1.06E-04 MIBK 1.40E-03 Ib/CDT (6) 2.02E+02 O.DOE+00 2.02E+02 1.01E-01 Methylene Chloride 3.50E-04 Ib/MMBtu (4) 1.84E+02 O.00E+00 1.84E+02 9.21E-02 n-Hexane 2.88E-04 Ib/MMBtu 4 1.80E+00 1.52E+02 2.97E+01 1.81E+02 9.06E-02 Naphthalene 7.44E-05 Ib/MMBtu (4) 6.10E-04 45% 2.15E+01 5.54E-03 2.15E+01 1.08E-02 Nickel 3.45E-06 Ib/MMBtu (5) 1.82E+00 O.00E+00 1.82E+00 9.08E-04 Phenol 2.38E-01 Ib/hr (2) 1.12E+03 O.00E+00 1.12E+03 5.59E-01 POM 1.74E-04 Ib/MMBtu (7) 9.14E+01 O.ODE+00 9.14E+01 4.57E-02 Pro anal 3.20E-06 Ib/MMBtu (7) 1.68E+00 O.ODE+00 1.68E+00 8.42E-04 Pro ionaldeh de 9.30E-02 Ib/hr (2) 4.37E+02 O.00E+00 4.37E+02 2.19E-01 Selenium 5.11E-07 Ib/MMBtu (5 2.40E-05 2.69E-01 3.96E-04 2.69E-01 1.35E-04 Styrene 6.30E-05 Ib/MMBtu (4 3.31E+01 O.DOE+00 3.31E+01 1.66E-02 Toluene 2.34E-05 Ib/MMBtu 4 3.40E-03 1.23E+01 5.61E-02 1.24E+01 6.18E-03 x Iene 5.22E-06 Ib/MMBtu 4 2.75E+00 O.DOE+00 2.75E+00 1.37E-03 1.Emission factors based on AP-42,Fifth Edition,Chapter 1,Section 4.Taken from DAQ spreadsheet online.July 1998 2.Emission factors from RTO inlet stack testing 12/200S 3.Emission factors from Stack testing 10/2009.Assumed condensible PM2.5=condensible PM30 4.Emission Factors from NCASI TB 973,Table 7.1-Uncontrolled,February 2010 5.Emission Factors from NCASI TB 973,Table 7.2-Control:ESP,February 2010 6.Emission Factors from T8 771,Table 6.2.1 Southern Pine Furnish(Dry)Average Emissions,January 1999 7.AP-42 1.6 Wood Residue Combustion,September 2003 8.VOC emission factor:VOC as C from 2009 Method 25A test 9.VOC as VOC(wood firing)=VOC as propane+Formaldehyde as Formaldehyde+0.5'Methanol as Methanol 10.All PM after WET ESP assumed to be PMIO. 11.Acetone as propane and methanol as propane calculated and used for the WPPI VOC calculation purposes only. 12.WPPI VOC=VOC as propane+methanol+formaldehyde-0.65'methanol as propane-0.65'acetone as propane 13.PM2.5 was not measured in the 2009 test.We have applied the ratio of 0.86 PM2.5/PM10 from AP-42 Section 1.6,Table 1.6-1 to the tested filterable PM10 value. 14.NCASI emission factor database cumene emissions from fiberboard refiner wet wood(50%moisture) PB Plant Fire Pump Engine and Backup Generator Emissions Fire Pump Engine: Backup Generator: Fire Pump Engine Hrs of Operation: 27.6 hrs/yr Backup Generator Hrs of Operation: 11.2 hrs/yr Fire Pump MMBtu/yr 67.0 MMBtu/yr Generator MMBtu/yr 13.3 MMBtu/yr Capacity:347 hp-out*7000 Btu-in/hp-hr 2.429 MMBtu/hr Capacity:465 hp-out*2544.434 Btu-in/hp-hr 1.183 MMBtu/hr 2,429,000 Btu/hr*gal/141,000 Btu 17.2 gal/hr 1,183,161.81 Btu/hr*gal/141,000 Btu 8.39 gal/hr Fire Pump Engine Generator Compound Emission Factor(l) Actual Emissions Compound Emission Factor(l) Actual Emissions Ib/MMBtu Ib/yr tPY Ib/MMBtu Ib/yr tPY PM 3.10E-01 2.08E+01 1.04E-02 PM 3.10E-01 4.11E+00 2.05E-03 PM10 3.10E-01 2.08E+01 1.04E-02 PM10 3.10E-01 4.11E+00 2.05E-03 PM2.5 1.30E-01 8.73E+00 4.36E-03 PM2.5 1.30E-01 1.73E+00 8.63E-04 SO2 2.90E-01 1.94E+01 9.72E-03 SO2 2.90E-01 3.84E+00 1.92E-03 NOx 4.41E+00 2.96E+02 1.48E-01 NOx 4.41E+00 5.84E+01 2.92E-02 VOC 3.60E-01 2.41E+01 1.21E-02 VOC 3.60E-01 4.77E+00 2.39E-03 CO 9.50E-01 6.37E+01 3.18E-02 CO 9.50E-01 1.26E+01 6.29E-03 Acetaldehyde 7.67E-04 5.14E-02 2.57E-05 Acetaldehyde 7.67E-04 1.02E-02 5.08E-06 Acrolein 9.25E-05 6.20E-03 3.10E-06 Acrolein 9.25E-05 1.23E-03 6.13E-07 Benzene 9.33E-04 6.25E-02 3.13E-05 Benzene 9.33E-04 1.24E-02 6.18E-06 Butadiene-1,3 3.91E-05 2.62E-03 1.31E-06 Butadiene-1,3 3.91E-05 5.18E-04 2.59E-07 Formaldehyde 1.18E-03 7.91E-02 3.96E-05 Formaldehyde 1.18E-03 1.56E-02 7.82E-06 Na thalene 8.48E-05 5.69E-03 2.84E-06 Na thalene 8.48E-05 1.12E-03 5.62E-07 POM 8.32E-05 5.58E-03 2.79E-06 POM 8.32E-05 1.10E-03 5.51E-07 Toluene 4.09E-04 2.74E-02 1.37E-05 Toluene 4.09E-04 5.42E-03 2.71E-06 Xylene 2.85E-04 1.91E-02 9.55E-06 X lene 2.85E-04 3.78E-03 1.89E-06 1.AP-42,Table 3.3-1 and 3.3-2,October 1996. PM2.5 is assumed to be 42%of PM per AP-42 Table 1.3-7 Diesel Heating Value: 0.141 MMBtu/gal PB Plam Ba6house Emission PB PIant ProduM1on. 136,575 BDT/y, RerNed VOC Tan pmuN Mnual Rnual Mnual KeMI Nnun i MmalPM30RTan N0110I Mnwl TOMI PM Ten TMProcea PM TertFmM1sbnllnual Mnual VIX McMad 254 Emhsbn Preue NC110 McMaml /PM2.5 RaR fatmr reduttlen Tem Remnnce EmisWHoun Ib/Ir j1I b/hrn W/Mn111 Ib/mn1�� Fmlaalens Eminbm Ib/hr"I w/m Is Ib/mna4 5599 W OTV EF 0.362 I.IOF-0 1)140 1bOE-01 10 896 6.50E-03 )W 9.)5 uwdust 4.5 63)1 Ten Q958 BO 104 3.00E-02 53059 95 I.EDE-02 10 1340 1. 40.1 6.91E-03 53059 3.3K-0E .. 4.1 ) W OTV EF 0.230 946 4.)OE-02 I- O 111 110E-0110 %6I. fi00E-03 6 -03 0.M Tla 3535 Mwoad warm a805 9 TestS 0.66E 103M 8.61E-02 1A 0022 Ills O.00EbO ]0 0 1649 5.32 6.10E-03 ) I.8 I O.OISfelmmam LMmt 515 h aandndml 4805 ]D16E W IEF 0.189 343) 1.58E-01 8298 0.038 .2 1.30E-01 10 1% 4136 1.K 8.3K-03 6- 2.00E-03 0.02 SanOerdust Tnm f 3%5 M s,nenemt 4805 S 3 TeslS 0.251 /3)6 4.31E-02 2W0 0.042 32] 1.30E-01 10 ]I 605 O.K fi20E-01 2 5.9%-01 1.64 Board...Tramin 3555 dr sawtlust 4805 ))3 I_, 0.110 33M 1.30E-01 13)6 -2 61 1.30E-02 /0 36) 3- 1.6) 4.51E-03 )fi ).0)F-04 21.0 0.01 Sandndusl Sib 35)5 dr sandndmf 4805 ]3]5 W oN EF 0.252 Im 5 5 0.0E2 6 30] 1.30E-01 10 % 116) 1.K 5 5 4.00E-01 950 14. Flakes 3585 tlr Oakes 4805 805)9 We o1V EF 0.140 11361 5 5 0.001 6 110 8.60E-03 ]0 693 11391 5.)0 5 5 2.00E 1 6 12I.o R.ol Finn Tram 3595 dr sawdust 4805 5463 W oNEF 0.140 )6S 5 5 0.002 6 1] 1.60E-01 10 8) ])6 0.39 5 5 3.36E-04 6 12 0m p Mafnul Tram 35]) wood wane 4805 41519 [nlmam 0.861 15.1" 5 5 0.032 11) 1.60E-01 ]0 6N %1K 16.4 5 5 2.08E-03 K.3 0.04 TMw l uwatlD ew.bwa neM to nOM,aM aEeO.eM Ia M.ptlrtatl.Mud m rvaep sub,wtad Ott 2001 IIE wl.dl ODlw olm bnnrw n sM kl 31 VOE wnedbVOC.tarbon eeuiwleinllem valans mxsurted MEP4 MnMd 2.,wnhF don roldauw lormeldeeyel N1H01 31 W um of MnbW ISa wnHLwn and Iwmalde6rh maldelrvde eminlam�atlMd de«rl�o vOC n VOC wlw.dw.elaa slue In uNe IMWe Iwmleange. 51 No end wm Int raMatM ]IE r nlln n999% EI F mhclwn nncM1.ar awn�lee Iw lablc Into at 99.99N. amnum al marenal woces+ed tbru n<n unit Malnter Is cnculnee M W m x M total mewlal wcmud M mill PB Plant Short Cycle Laminating Press Emissions Actual 2015 Actual VOC l Process Annual 2015 Actual Annual Emissions Formaldehyde PM Emission PM-10 Emissi PM on Annual VOC Annual VOC Actual Annual Annual Total Actual Annual Annual PINI Actual PM-I() PM-30 PM-2.5 PM-2.5 Source 10 No. Emission Factor Emission Emissions Emissions Formaldehyde VOC PM Emissions Emissions Emissions Emissions Emissions Material Operating Production(MSF) Factorlb/hr Factorlb/hr Factor Emissions Hours )1) Ib/hr(2) Factor lb/hr Ib/hr Ib/yr ton/yr Emissions lb/yr Emissions Ib/yr ton/yr Ib/yr ton/yr Ib/yr ton/yr lb/yr13) Wemhoner Short Cycle Paper 3593 6.938 26,765 0.016 0.02 0.86 065 0.31 95.008 0.048 119 213.767 5,307 2.553 3,266 1.633 1,841 0.920 Laminating Press Trimmings Steinemann Short Cycle Paper Laminatin Presses 3594 Trimmin s 0 0 0.016 0.02 0.86 0.55 0.31 0 0.000 0 0.00 0 0.00 0 0.00 0 0.00 11 Emission estimates from a similar source.The similar press is 9MM m2/yr,whereas Uniboard's press has a design of approximately 17.6 MM m2/yr,therefore,emission factors from similar source are multiplied by 1.95313 21 Emission estimates from a similar source 3)Total VOC as VOC calculated using converted VOC-carbon equivalent emissions from the sum of Method 25A emissions and formaldehyde emissions.Formaldehyde emissions are added directly to VOC as VOC value,therefore values in table include formaldehyde. The two presses are identical and have identical emissions. PB Plant Laiminator Thermal Oil Heater(Pr-Heatl)-Natural Gas Fired or No.2 Fuel Oil Diesel Usage: 0 gal/yr Compound Factor(1) Emissions Ib/M al Ibs/ r tons/year Filterable PM(FPM) 2.00E+00 0.00E+00 0.00E+00 Condensible PM(CPM) 1.30E+00 0.00E+00 0.00E+00 Total Particulate Matter(PM)(FPM+CPM) 3.30E+00 0.00E+00 0.00E+00 Filterable PM<10 Microns(PMIo) 1.00E+00 0.00E+00 0.00E+00 Total PMIo 2.30E+00 0.00E+00 0.00E+00 Filterable PM<2.5 Microns(PMz 5) 2.50E-01 0.00E+00 0.00E+00 Total PM2 s 1.55E+00 0.00E+00 0.00E+00 Sulfur Dioxide(S02) 7.10E+01 0.00E+00 0.00E+00 Nitrogen Oxides(NOx) 2.00E+01 0.00E+00 0.00E+00 Carbon Monoxide(CO) 5.00E+00 0.00E+00 0.00E+00 Volatile Organic Compounds(VOC) 2.00E-01 0.00E+00 0.00E+00 Arsenic&compounds 5.60E-04 0.00E+00 0.00E+00 Benzene 2.75E-03 0.00E+00 0.00E+00 Beryllium&compounds 4.20E-04 0.00E+00 0.00E+00 Cadmium&compounds 4.20E-04 0.00E+00 0.00E+00 Chromium-All/Total 4.20E-04 0.00E+00 0.00E+00 Ethylbenzene 8.17E-04 0.00E+00 0.00E+00 Fluorides(sum fluoride compounds) 3.73E-02 0.00E+00 0.00E+00 Formaldehyde 4.80E-02 0.00E+00 0.00E+00 Lead and Lead compounds 1.26E-03 0.00E+00 0.00E+00 Manganese&compounds 8.40E-04 0.00E+00 0.00E+00 Mercury&compounds 4.20E-04 0.00E+00 0.00E+00 Methyl chloroform 2.36E-04 0.00E+00 0.00E+00 Naphthalene 3.33E-04 0.00E+00 0.00E+00 Nickel&compounds 4.20E-04 0.00E+00 0.00E+00 POM rates uncontrolled 3.30E-03 0.00E+00 0.00E+00 Selenium compounds 2.10E-03 0.00E+00 0.00E+00 Toluene 7.97E-02 0.00E+00 0.00E+00 X lene 1.40E-03 0.00E+00 0.00E+00 1.Emission factors from NC DAQ's fuel oil spreadsheet-based on AP-42,5th edition,Section 1.3. *Only fired No.2 Oil in 2010 Natural Gas Usage 6.602 MMSCF/ r Compound Emission Factor Reference Emissions, Emissions, Ib r t NG dung for Lwdneft presm Illunflng NG NOx 5.00E+01 Ib/mmscf (2) 3.30E+02 1.65E-01 CO 8.40E+01 Ib/mmscf (2) 5.55E+02 2.77E-01 PM/PM10/PM2.5 7.60E+00 Ib/mmscf (2) 5.02E+01 2.51E-02 S02 6.00E-01 Ib/mmscf (2) 3.96E+00 1.98E-03 VOC 5.50E+00 Ib/mmscf (2) 3.63E+01 1.82E-02 Benzene(71-43-2 TH) 2.10E-03 Ib/mmscf (2) 1.39E-02 6.93E-06 Benzo(a) rene (50-32-8 T) 1.20E-06 Ib/mmscf (2) 7.92E-06 3.96E-09 Cobalt compounds(H) 8.40E-05 Ib/mmscf (2) 5.55E-04 2.77E-07 Formaldehyde(50-00-0 TH) 7.50E-02 Ib/mmscf (2) 4.95E-01 2.48E-04 Hexane 1.80E+00 Ib/mmscf (2) 1.19E+01 5.94E-03 Naphthalene (91-20-3 H) 6.10E-04 Ib/mmscf (2) 4.03E-03 2.01E-06 Selenium compounds(H) 2.40E-05 Ib/mmscf (2) 1.58E-04 7.92E-08 Toluene(108-88-3 TH) 3.40E-03 Ib/mmscf (2) 2.24E-02 1.12E-05 2.Emission factors based on AP-42,Fifth Edition,Chapter 1,Section 4.Taken from DAQ spreadsheet online.July 1998 = u y Ponds 2-5 and Spray Field Fugitives Ponds 2-5 Fugitives Spray and Pond Concentration:1 0.2 mg/L Spray and Pond Concentration(converted):Z 1.67E-06 lb/gal Total Pond Capacity: 2,879,000 gal/yr Fugitive Emissions, Fugitive Emissions, Compound Emission Factor Ib/yr tpy Ponds 2-S and Spray Fields VOC 0.2 mg/L 1 4.8 2.40E-03 Formaldehyde(50-00-0 TH) 0.2 mg/L 1 4.8 2.40E-03 1.Concentration from 2011 Formaldehyde test.Using half of detection limit since concentration was below the detection limit of 0.4 mg/L. Spray Field Fugitives Spray and Pond Concentration:1 0.2 mg/L Spray and Pond Concentration(converted):z 1.67E-06 lb/gal Total Gallons Irrigated: 11,943,000 gal/yr Fugitive Emissions, Fugitive Emissions, Compound Emission Factor Ib/yr tpy Ponds 2-5 and Spray Fields VOC 0.2 mg/L 19.9 9.97E-03 Formaldehyde(50-00-0 TH) 0.2 mg/L 19.9 1 9.97E-03 1.Concentration from 2011 Formaldehyde test.Using half of detection limit since concentration was below the detection limit of 0.4 mg/L. r Cure Formaldehyde Units Methanol Units Production Ratio Units 3.2 Process the toxic chemical 5.1 Fugitive Emissions 58 Ibs 40 Ibs Bypass Events-Wellons,PB Press,Teaford abort 5.2 Stack or Point Emissions 254,776 Ibs 52,292 Ibs All Process Units Except Tank Working Waste and Bypass Events 5.5.2 Land Treatment/Application Farming 20 8.1b Total Other On-Site Disposal or Releases 0 Ibs 0 Ibs 8.6 Total Treated 2,443,249 Ibs 306,998 Ibs Total emissions routed through HAPs control 8.9 Production Ratio 1.08 2015 m3/2014 m3 2014 PB Production m3 251,404 2014 MDF Production m3 231,881 2015 PB Production m3 259,495 2015 MDF Production m3 261,698 M : J L PB Plant Gasoline Tank Emissions(l) Total VOC Emissions"', Ibs: 11 Total VOC EmissionslZl,tons: 0.01 Throughput,Gallons: 0 Actual Hours of Operation: 8784 Vapor Weight Emissions Compound(3) Percent(3) Ibs/ r t pY Benzene 3.25% 0.35 1.74E-04 Chlorobenzene 0.03% 0.00 1.61E-06 Cumene 0.33% 0.04 1.77E-05 Ethyl benzene 4.07% 0.44 2.18E-04 Hexane,n- 3.91% 0.42 2.09E-04 Naphthalene 0.80% 0.09 4.28E-05 Styrene 0.17% 0.02 9.10E-06 Toluene 15.22% 1.63 8.14E-04 Trimethyl pentane 0.68% 0.07 3.64E-05 X lenes 21.69% 1 2.32 1 1.16E-03 Total 5.37 2.68E-03 Notes: (1)RVP-10 gasoline 270 gallon,outside,above-ground tank,painted white put into service mid-2003 (2) Emissions estimated by EPA Tanks Program,V.4.09d (3) EPA SPECIATE database in AIRCHIEF,Oct. 1993. r y Facility Name Arauco Panel USA, LLC Facility ID 1900015 North Carolina Department of Environment and Natural Resources Division of Air Quality General Information If any information already provided to DAQ has changed or otherwise is incorrect,please provide corrections. You may leave blanks where the information is unchanged. (Except Facility ID and Name). Physical(911)Address of Facility 985 Corinth Road Moncure,NC 27559 Name of Responsible Official—HqM Scheller Title Plant Manager Telephone# (919) 642 - 6600 E-Mail Address henry.scheller@arauco-na.com Mailing Address of Responsible Official_985 Corinth Road Moncure,NC 27559 Name of Facility Technical/Permit Mailing Contact Yvonne Couts Title Environmental Coordinator Telephone# (919) 545 -_5848_ E-Mail Address yvonne.couts(iDarauco-na.com Mailing Address of Responsible Official 985 Corinth Road Moncure,NC 27559 Name of Inspection Contact Title Telephone# ( � - E-Mail Address Name of Billing/Invoice Contact_Henry Scheller Title Plant Manager Telephone# 19 9 _642_- 6600 E-Mail Address Billing/Invoice Company Billing/Invoice Address Standard Industrial Classification (SIC) Code(s) 2493 North American Industry Classification System 321219 (NAICS—six digit) Code(s)— If known (see instructions) Report Prepared by Yvonne Couts Telephone# (_919) 545 - 6600 E-Mail Address yvonne.coutskarauco-na.com Provide to Appropriate DAQ Regional Office as needed. Information on This Form cannot be held confidential. North America 985 Corinth Road Tel: 919.542.2828 ARAUCO. Moncure, NC 27559 Fax: 919.642.6600 www.arauco-na.com August 24, 2017 Mr. Matthew Mahler Engineer 3800 Barrett Drive Raleigh, NC 27609 Subject: 2016 Annual Emissions Inventory Summary Mr. Matthew Mahler, As per our conversation today (August 24, 2017) Arauco is resending the 2016 Annual Emissions Inventory Summary sheet in a form that is more legible. If this font size is still too difficult to read please reach out to me again. I can be contacted at 919-545-5848 ext. 25848 or yvonne.couts@arauco-na.com Sincerely, - , vonne Couts Environmental Coordinator NC Dept of F,nvironmental Quality 2017 Raleigh Rcbional Office a ity An e Tffr& JL)Ilal Ullice