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HomeMy WebLinkAboutAQ_F_1900039_20170614_EI_Cmb-EI-File jr `f 2016 Emissions Inventory Review / Data Tracking Form Facility Name: Moncure Plywood FacRi ID: 1900039 Facility Assigned to: Data Entry: Chatham County Classification: Matthew Mahler /o_ 1,f — 0 Confidential Copy Submitted? Title V ❑ YES �NO Initial Review/Data Entry Enter date received into ED. Date Received: 6 —1 — t-7 ❑ 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 011"Electronic copy submitted: All supporting documentation and certification form(with time/date stamp)signed by responsible official has been received. Comments: co e issior., IKCr2w5e- Lot 4 (V�c ,ef,S �eKeer dw�c� �(,�rwtill P.f —30. �1'Qsl T6�1�-s A-g 2ea5e Jae- 4v hiaJlntr 4 .,,Rk n�T a� %fe^-Q e; CL4 ers (©5-'2 G -to 0 s - 31) . Inventory Review D"' All forms and supporting documentation appear to be complete if paper submission(check ED OS data if electronic). [3,*�Contact,address,phone number changes entered into I-Beam/Facilities if necessary. M"'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. Q"Check if SCC codes for each OS are accurate and update if needed. Evaluate"U"sources for significance and address according to policy. Calculations/forms appear to add up correctly. GKAll compliance issues are being addressed(e.g.Toxics limits,above TV thresholds,large emissions increase/decrease,installation without a permit). G'All volatile HAPs/TAPS were included in the VOC total. . Q�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.). L"J Review facility comments and address any issues. 53"' Update ED(Data Entry Main)if additional information is required(corrections due date and date received). IV Check all ED QA/QC reports. rComparison with previous emission inventory must be made and outliers(> 10%)must be investigated and explained. V,L� ut 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: / U — 15 —" / Signature: G7✓f Date Submitted to EI Coordinator: l l 7— 1 7 Date Approved: b/ l '� Initials: 1�� /19 C.114 Boise Cascade Moneure Plywood 306 Corinth Rd. Moncure,NC 27559 (803)-3854957 June 19, 2017 Mr. Patrick Butler Raleigh Regional Office 3800 Barrett Drive Raleigh,NC 27609 Subject: Final 2016 Air Emissions Inventory for Boise Cascade—Moncure Plywood I have enclosed two copies of the subject report for your review. Also please find the General Information page indicating that Chris Seymour, Southeast Area Manager is the responsible official. Should you have questions, Please call Brian Van Gelder, Environmental Manager, at(803) 385-4957. Sincerely, Tony Neely y Environmental Coordinator t Of nvir �pn 111CDePtopEmental Qualify Hal mental Quality Raleigh Reg k g l°nal O tfic e Facility Name_Boise Cascade Wood Products - Moncure Plywood Facility ID 1900039_ 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 Name of Responsible Official Chris Seymour Title Southeast Area Manager Telephone# U - E-Mail Address ChrisSeymour@bc.com Mailing Address of Responsible Official Name of Facility Technical/Permit Mailing Contact Title Telephone # ( ) - E-Mail Address Mailing Address of Responsible Official Name of Inspection Contact Title Telephone # (� - E-Mail Address Name of Billing/Invoice Contact Title Telephone#(� - E-Mail Address Billing/Invoice Company Billing/Invoice Address Standard Industrial Classification (SIC) Code(s) North American Industry Classification System (NAICS—six digit) Code(s)— If known (see instructions) ental Ual'ty NC Dept° ' Report Prepared by Telephone# E-Mail Address 11 `V Provide to Appropriate DAQ Regional Office as neigh Rcg1Onal Office Information on This Form cannot be held confidential. Comments from AERO Submitter 1900039: Moncure Plywood 2016 Inventory Year Archived Comments Emission Release Point Comments 6/14/17 General Comments 1.Some criteria pollutant emissions for OS-2,OS-3,OS-4,OS-6,OS-16,OS-24,OS-25,OS-34,OS-36,and OS-37 are below the AERO reporting threshold;see emissions in calculations. 2.Remove OS-35,as same as OS-37,for#2 fire water engine. t 1 Facility Total CY 2016 Emission Summary Recorded in ED Facility ID#: 1900039 Facility Name: Moncure Plywood Permit#(s): 03424725 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 33.94 26.61 0.5 27.5% NOx NOx 40.82 44.84 0.5 -9.0% PM(TSP) TSP 59.06 60.75 0.5 -2.8% PM10 PMIO 5 8.8 1' 60.73 0.5 -3.2% PM2.5 PM2.5 51.71 51.38 0.5 0.6% SO2 3O2 0.650000 0.710000 0.5 -8.5% VOC VOC 64.64 63.28 0.5 2.1% 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 1.29 1.41 0.01, I -8.5% all inorganic compounds) Arsenic Unlisted Compounds.-Specify Compound ASC-Other 1.29 1.41 0.01 -8.8% (Component of ASC) Cadmium&compounds(total mass includes elemental metal) 1.91 Z09 0.1 -8.6% Cadmium Metal,elemental;unreacted(Component of 7440-43-9 1.91 2.09 0.1 -8.8% CDC) Cadmium Unlisted Compounds-Specify Compound CDC-Other Not 0.000120 0.1 N/A (Component of CDC) Reported Chromium-AIUTotal(includes Chromium(VI) categories, 12.41 13.61 0.1 I -8.8% metal and others) Chromic acid(VI)(Component of So1CR6&CRC) 7738-94-5 2.79 3.06 0.01 -8.8% 10/18/2017 Page 1 of 4 Facility Total CY 2016 Emission Summary Recorded in ED Facility ID#: 1900039 Facility Name: Moncure Plywood Permit#(s): 03424T25 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 Unlisted Compounds-Specify Compound CRC-Other 9.62 10.55 0.1 -8.8% (Component of CRC) Chromium(VI)Soluble Chromate Compounds(Component of 2.79 3.06 0.01 -8.8% CRC) Chromic acid(VI)(Component of So1CR6&CRC) 7738-94-5 2.79 3.06 0.01 -8.8% Lead&compounds 6.17 6.77- 1.0 I -8.9% Lead Unlisted Compounds-Specify Compound PBC-other 6.17 6.77 -10.0 -8.8% (Component of PBC) Manganese&compounds 998.04 1,094.17 10.0 -8.8% Manganese Unlisted Compounds-Specify Compound MNC-other 998.04 1,094.17 10.0 -8.8% (Component of MNC) Mercury& Compounds-all total mass includes Hg Vapor 0.460941 0.505620 0.001 -8.8% Mercury,vapor(Component of HGC) 7439-97-6 0.460941 0.505620 0.001 -8.8% Nickel& Compounds,sum total mass includes elemental 4.69 5.14 1.0 I -8.8% Nickel metal(Component of NIC) 7440-02-0 4.69 5.14 1.0 -8.8% Nickel Unlisted Compounds(Component of NIC- NIC-Other Not 0.000220 1.0 N/A Specify) Reported Polycyclic Organic Matter(Specific Compounds from OAQPS 3.26 3.58 1.0 -8.9% or T P) Naphthalene(Component of 83329/POMTV) 91-20-3 3.26 3.58 1.0 -8.8% Acetaldehyde 75-07-0 2,173.85 -1,974.49 10.0 1.0.1% Acrolein 107-02-8 321.75 335.18 10.0 -4.0% Benzene 71-43-2 179.45 175.40 1.0 2.3% Carbon tetrachloride 56-23-5 1.02 1.12 1.0 -8.8% Chlorine 7782-50-5 316.65 347.15 100.0 -8.8% Cumene 98-82-8 1,713.09 1,368.48 100.0 25.2% Ethyl chloride(chloroethane) 75-00-3 46.05 36.79 10.0 25.2% Ethylene dichloride(1,2-dichloroethane) 107-06-2 70.59 56.39 1.0 25.2% 10/18/2017 Page 2 of 4 I Facility Total CY 2016 Emission Summary Recorded in ED Facility ID#: 1900039 Facility Name: Moncure Plywood Permit#(s): 03424T25 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 Formaldehyde 50-00-0 2,632.32 2,320.88 10.0 13.4% Hydrogen chloride(hydrochloric acid) 7647-01-0 138.68 152.04 100.0 -8.8% MEK(methyl ethyl ketone,2-butanone) 78-93-3 149.63 Not 100.0 N/A Reported Methanol(methyl alcohol) 67-56-1 13,445.44 14,181.18 1,000.0 -5.2% Methyl bromide(bromomethane) 74-83-9 67.67 54.04 1.0 25.2% Methyl chloride(chloromethane) 74-87-3 10.66 11.69 1.0 -8.8% Methylene chloride 75-09-2 60.62 48.43 1.0 25.2% MIBK(methyl isobutyl ketone) 108-10-1 191.95 171.06 10.0 12.2% Phenol 108-95-2 1,184.20 1,378.08 100.0 -14.1% Phosphorus Metal,Yellow or White 7723-14-0 2,184.47 2,394.87 1.0 -8.8% Polycyclic Organic Matter(Inc PAH,dioxins,etc.NC POM 8.95 9.81 1.0 -8.8% &AP 42 historic) Propionaldehyde 123-38-6 105.44 67.64 10.0 55.9% Trichlorobenzene, 1,2,4- 120-82-1 129.39 103.34 100.0 25.2% Vinyl chloride 75-01-4 44.51 35.56 0.1 25.2% Vinylidene chloride 75-35-4 67.38 53.39 0.1726.2% Xylene(mixed isomers) 1330-20-7 123.13 110.62 100.0 11.3% 10/18/200 Page 3 of 4 Largest Individual HAP Methanol(methyl alcohol) 13,445.44 lbs Total HAP Emissions 26,245.51 lbs Largest Individual CAP VOC 64.64 tons Total CAP Emissions 198.86 tons Total TAP Emissions 8,663.64 lbs Total Aggregate 199.12 tons Emissions DAO's Comments Regarding Inventory CO emissions increase due to increased veneer dryer throughput,OS-30. HAPs/TAPs increase due to higher throughput of veneer dryers(OS-26 to OS-31). 10/18/2017 Page 4 of 4 2016 NORTH CAROLINA AIR EMISSIONS INVENTORY Prepared for: (T Boise Cascade Boise Cascade Wood Products - Moncure Plywood 306 Corinth Road Moncure,North Carolina 27559 Prepared by: A=COM 1600 Perimeter Park Drive, Suite 400 Morrisville, North Carolina 27560 (919)461-1100 AECOM Project No. 60542933 June 2017 OF • Inventory Certification Letter A Facility Summary B i Emission Sources, Control Devices, C and Operating Scenario Lists AERO Emission Forms and Calculations D Supporting Data E I i { I Appendix A Inventory Certification Letter ti i COPY of RECORD Date Submitted: 6/14/2017 13:28:13 Inventory Certification Form(Title V) Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit: 03424 Moncure,NC 27559 County: Chatham . DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 These forms must be completed and returned even if the facility did not operate or emissions were zero The legally defined "Responsible Official' of record for your facility is Bill Kopp This person or one that meets the definition below must sin 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: (Importants Legally i le re final. I 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 enalities 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: CO- I q - z o►Z Printed Name: Bill Kepp Chris Seymour Sign re: ` This form app s to Title NCfadliiies. 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: billkepp@be.eem ChrisSeymour@bc.com Information on this Form cannot be held confidential COPY of RECORD Date Submitted: 6/14/2017 1128:13 1 i i i I J Appendix B Facility Summary J�� Facility Total CY 2016 Emissions Summary COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit: 03424 Moncure,NC 27559 County : Chatham DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 Record Facility—Wide Totals From all Permitted and Non—Permitted Air Pollutant Emission Sources Green House Gases Pollutants(GHG) Actual Emissions Tons/Year Pollutant CAS 1 2016 2015 Chan e Criteria Pollutants Actual Emissions (Tons/Year Pollutant CAS 2016 2015 % Change CO CO 33.94 26.61 27.546028% NOx NOx 40.82 44.84 —8.965211% PM TSP TSP 59.06 60.75 —2.7818906% PM 10 PM 10 58.81 60.73 —3.1615317% PM2.5 PM2.5 51.71 51.38 0.6422694% S02 S02 0.65 .71 —8.450705% VOC VOC 64.64 63.28 2.14917920/o Hazardous Air Pollutants HAPS and/or Toxic Air Pollutants TAPs Actual Emissions Pounds/Year Pollutant I CAS 1 2016 1 2015 % Change Pollutant Group:Arsenic Compounds(total mass of elemental AS, arsine and all inorganic compounds) Group Sum:1.290640073 Arsenic Unlisted Compounds( ASC—Other 1.2906401 1.41497 —8.786754% Specify Component of ASC Pollutant Grou :Cadmium compounds total mass inc elemental metal Group Sum:1.907900401 Cadmium Metal(elemental unreacted, Component of 7440-43-9 1.9079 2.09167 —8.785806% CDC Cadmium Unlisted Compounds CDC—Other 4.01 E-7 .00012 —99.66584% (Specify Component of CDC Pollutant Grou :Chromium VI Soluble Chromate Compounds(Component of CRC Group Sum:2.79372 Chromic acid(VI)(Component 7738-94-5 2.79372 3.06279 —8.785124% of SolCR6 CRC Pollutant Grou :Chromium—All/Total Inc Chromium VI categories,metal and Others Group Sum:12.413400511 Chromic acid(VI)(Component 7738-94-5 2.79372 3.06279 —8.785124% 76 of So1CR6 CRC Chromium Unlisted Compounds(Specify CRC-Other 9.61968 10.54635 -8.786634% Component of CRC - Pollutant Grou :Lead and Lead compounds Group Sum:6.172620182 Lead Unlisted Compounds (Specify and Component of PBC-Other 6.1726203 6.7672 -8.7862% PBC Pollutant Grou :Man anese com ounds Group Sum:998.041800139 Manganese Unlisted Compounds(Specify MNC-Other 998.0418 1094.16829 -8.785351% Component of MNC Pollutant Grou :Mercu Com ounds-all total mass inc Hg Vapor Group Sum:.460940948 Mercury,vapor(Component of 7439-97-6 0.46094096 .50562 -8.836487% HGC Pollutant Grou :Nickel Compounds, sum total mass, inc elemental Group Sum:4.689590766 Nickel Unlisted Compounds(Specify Component of NIC NIC-Other 7.66E-7 .00022 -99.65182% Nickel metal (Component of 7440-02-0 4.68959 5.14128 -8.78556% NIC Pollutant Grou :Pol c clic Or anic Matter(Specific Com ounds from OA PS for TV Group Sum:3.26414223 Naphthalene(Component of - p ( p 91-20-3 3.2641423 3.58044 -8.834047% 'i POMTV Acetaldehyde 75-07-0 2173.8499 1974.48828 10.096872% Acrolein 107-02-8 321.7512 335.18093 -4.0067163% Benzene 71-43-2 179.45425 175.39723 2.313048% Carbon tetrachloride 56-23-5 1.0221 1.12053 -8.78424% -- Chlorine 7782-50-5 316.6478 347.14575 -8.785346% Cumene 98-82-8 1713.0898 1368.47981 25.181957% Ethyl chloride chloroethane 75-00-3 46.04785 36.78663 25.175514% Ethylene dichloride 107-06-2 70.58717 56.38552 25.1867% 1,2-dichloroethane Formaldehyde 50-00-0 2632.3186 2320.88101 13.418934% Hydrogen chloride(hydrochloric acid 7647-01-0 138.68372 152.04105 -8.785345% Methanol 67-56-1 13445.437 14181.178 -5.1881533% Methyl bromide 74-83-9 67.66994 54.04487 25.21066% Methyl chloride 74-87-3 10.66181 11.68871 -8.785403% Methyl ethyl ketone 78-93-3 149.63388 Not reported N/A Methyl isobutyl ketone 108-10-1 191.94618 171.06168 12.208758% - Methylene chloride 75-09-2 60.622 48.42762 25.180635% Phenol 108-95-2 1184.2035 1378.07636 -14.068373% Phosphorus Metal,Yellow or 7723-14-0 2184.469 2394.86625 -8.785344% White Polycyclic Organic Matter(Inc PAH, dioxins, etc.NC AP 42 POM 8.949161 9.81367 -8.809238% -- historic amorphous lob Pro ionaldeh de 123-38-6 105.44087 67.63753 55.89108% Trichlorobenzene, 1,2 4- 120-82-1 129.39188 103.33796 25.212337% Vinyl chloride 75-01-4 44.5*1152 35.55893 25.176773% 77 Vin lidene chloride 75-35-4 67.37705 53.3879 26.202848% X lene 1330-20-7 123.1327 110.6151 11.316359% 78 COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit: 03424 Moncure,NC 27559 County : Chatham DAQ Region : RRO Comments From Facility: 5/30/2017—General Comments General Comments : 1. Some criteria pollutant emissions for OS-2, OS-3,OS-4,OS-6,OS-16,OS-24,OS-25, OS-34, OS-36,and OS-37 are below the AERO reporting threshold; see emissions in calculations. 2. Remove OS-35, as same as OS-37, for#2 fire water engine. 79 Boise Cascade Wood Products-Moncure Plywood Facility-Wide Summary of Actual Emissions 2016 Air Emissions Inventory FBB& Dry Waste Sander Gr.Veneer Hammer Hog Dry Waste Compound Dryers Storage System Stackers Truck Dump Truck Dump Emissions Emissions t ES-1910 ES-12 ES-04 IS-IN-9&10 IS-IN-11 IS-IN-12 Ib/ r tons/ r CO 33.90 67,851 33.93 Ox 40.68 81,644 40.82 PM 33.84 0.41 0.12 0.54 0.00 0.00 118,152 59.08 PMIO 33.84 0.41 0.12 0.54 0.00 0.00 117,633 58.82 PM2.5 33.17 0.41 0.12 0.00 0.00 103,433 51.72 VOC 44.66 1.54 129,335 64.67 S02 0.64 1,293 0.65 Compound Emissions DeMinimus Report in (lb/yr) Ib/yr (lb/yr) AEI? Acetaldehyde TH 1598.31 35.97 2,173.85 10 Yes Aceto henone H) 0.74 0.74 100 No Acrolein TH 321.75 321.75 10 Yes Antimonv&Compounds (H) 1 39 1.39 10 No Arsenic&Compounds TH 1 29 1.29 0.01 Yes Benzene TH 179.42 179.48 1 Yes Benzo(a) ene T) 0.01 0.01 I No Beryllium Compounds(TH) 0.02 0.02 1 No Cadmium Compounds 1.91 1.91 0.1 Yes Carbon tetrachloride TH 1.02 1.02 1 Yes Chlorine 316.65 316.65 100 Yes Chlorobenzene(TH) 6.65 6.65 10 No Chloroform(TH) 1.02 1.02 100 No Chromium-Other com H 9.62 9.62 0.1 Yes Chromium VI Compounds TH 2.79 2.79 0.01 Yes Cobalt compounds(H) 0.85 0 85 1 No Cumene H 1712.52 1,712.52 100 Yes Dinitro henol,2,4- H 0.05 0.05 0.1 No Di(2-eth (hex I) hthalate(DEHP)(TH) 0.02 0.02 10 No Ethyl benzene(H) 12.55 12.55 100 No Ethyl chloride chloroethane i,11, 46.01 46.01 10 1 Yes Ethylene dichloride(fI 11 70.53 70.53 1 Yes Formaldehyde(TH) 2162.63 _4.79 2,632.32 10 Yes Hexachlorodibenzo- dioxin 1,2,3,6,7,8(T) 0.00 0.000001 0.00001 No Hexane(TH) 0.01 0.01 100 No Hydrogen chloride 138.68 138.68 100 Yes Lead and Lead compounds H 6.17 6.17 1 Yes Manganese&compounds TH 998.04 998.04 10 1 Yes Mercury Compound TH 0.46 0.46 0.001 Yes Methanol H 2806.09 1;7(17 13,445.44 1000 Yes Methyl bromide H 67.63 67.63 1 Yes Methyl chloride H 10.66 10.66 1 Yes Methvl chloroform(TH) 15.75 15.75 100 No Methyl ethyl ketone T 115.01 149.35 100 Yes Methyl Isobutyl Ketone TH 157.34 191.89 10 1 Yes Methylene chloride 60.55 60.55 1 Yes Naphthalene H 3.26 3.26 1 Yes Nickel Compounds(TH) 4.69 4.69 1 Yes Nitro phenol-4-(11) 0.04 0.04 10 No Pentachloro henol TH 0.02 0.02 1 No Perchloroeth lene TH 9.86 9.86 100 No Phenol 328 11 1,194.49 100 1 Yes Phosphorus Metal,Yellow or White H '184 47 2,184.47 l Yes Polychlorinated bi hen Is TH a 00 0.003 t0 No Pol c clic Organic Matter 894 8.95 1 Yes Pro ionaldeh de H 105.38 105.38 10 Yes Propylene dichloride H 6.73 6.73 10 No Selenium compounds 0.22 0.22 10 No Styrene TH 45.62 45.62 100 No Tetrachlorodibenzo- dioxin,2,3,7,8- (TH) 0.00 0.000001 0.00001 No Toluene TH 39.27 39.29 100 No l richlorobenzene,1,2,4 11944 129.44 100 Yes l richloroeth lene TH 7'M 7.98 1000 No frichlorofluoromethane CFC I11 T 6,7 6.37 100 No Trichloro henol,2,4,6- H 0.1 1 0.11 1 No Vinyl acetate H) L34 100 No Vinyl chloride 44.55 44.55 0 1 Yes Vin lidenechloride 1,1-dichloroethene TH 67.42 67.42 u I Yes X lene(TH) 123.06 123.08 100 Yes I� I � II y Appendix C Emission Sources, Control Devices, and Operating Scenario Lists �I COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit: 03424 Moncure,NC 27559 County.: Chatham DAQ Region :RRO Listing of Emission Sources and Control Devices on Permit. See instructions ES ID on ES Description sCS ID CS Description CD ID's Air Permit ES-13-25HP 25 panel hot press ES-13-40HP 40 panel hot press ES-13—CC Curtain coater ES-13—PO Paper overlay operation ES-13—PS Plywood s reader Fluidized bed wood burner with blending chamber and ESO1—A dedicated overtire air fan(80.0 CS-1 multicyclone CDO2 million Btu/hr heat input capacity) Boiler(29.79 million Btu/hr ESOI—B heat input capacity,based on CS-1 multicyclone CD02 slipstream gas from ID No. ES-01—A) [NSPS Subpart Dc] ES03—CC Core composer with saw ES03—CS Core saw(green or dry veneer) ES03—PSS Panel sawing system ES03—SMS-1 String machine including saws CS-3 bagfilter(7,095 square feet of filter CD03—WWTC,CD06 area), dry waste transfer cyclone ES03—SMS-2 String machine including saws ES03—SS Strip saw Bagfilter(6,200 square feet of filter ES04 Wood sander CS-10 area),Woodwaste transfer cyclone(154 CD05,CD03—WWTC, inches in diameter),Bagfilter(7,095 CD06 square feet of filter area), ES09 M�2 t wood—fired veneer dryer C-S-1 multicyclone CD02 ES10 . M�2 t wood—fired veneer dryer CS-1 multicyclone CD02 ES12 Dry wood residual storage silo CS-5 cartridge filter(1,800 square feet of CD21 filter area) Glue mixing operations ES 13—GMO consisting of two resin storage tanks and four mixed glue tanks 2 Cyclone(60 inches in Rechip_blow hog(green wood diameter),Woodwaste transfer cyclone CD18;CD03—WWTC, ES14 CS-12 _. 154 inches_in_diameter ,Ba filter _CD06_ ---- -------. -- . _only)----- -- - --- - - - - - --- ---- -- - - (-- -- - - - )- g - - _ - - _---- -- ----' (7,095 square feet:of filter area), bagfilter(7,095 square feet of filter ES16 Plywood waste hog CS-3 CD03=WWTC, CD06 area),dry waste transfer cyclone Cyclone(60 inches in _ Green wood sizing operations. diameter),Woodwaste.transfer cyclone -CD18;CD03—WWTC, ES17 including sizing screens and-.. CS-12 054 inches in diameter),Bagfilter CD06 bins . (7,095 square feet of filter area), . ES20 Vat operations ES21 Edge sealer spray.booth Tongue and groove saw bagfilter(7,095 square feet of filter ES22 CS-7 CD06 ' (plywood.finishing) area) I-1 Bark hogging operations with two saws green wood Veneer stacker No. I-10 2 . I-11 hammer hog truck dump I-12 dry waste truck dump 17-2 Core:chipping and handling I-3 Green veneer hogging I-4 Logo painting and ink marking I-5 Logo painting and ink marking I-6 Plywood surface patching I-7 Maintenance parts washers 1_8 Veneer diverter exhaust cyclone I-9 green wood veneer stacker No. W 1 � Diesel—fired water pump(250 Horsepower maximum power IES-19 output):for emergency purposes f only[Area Source MACT ZZZZ] Diesel-fired fire pump N emergency engine(250 IES-23 Horsepower maximum power output)for emergency purposes only [Area Source MACT ZZZZ,NSPS Subpart I1II] IES—GWS 10reen wood fuel storage silo 3 COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit : 03424 Moncure,NC 27559 County: Chatham DAQ Region : RRO Emission Source & Operating Scenario List — See Instructions *ES Group ID *ES ID OS ID *OS Description GR2 I-10,I-9 32 Green Veneer Stackers 26 Veneer dryers and heat source(wood burner)lbs/SF, (Softwood) 27 Veneer dryers and heat source(wood ESO1—A ESO1—B burner)HAPS lb/mmBtu,(Softwood) _ 24 ES09 ES10 30 Veneer dryers and heat source(wood ' burner) lbs/SF,(Hardwood) 31 Veneer dryers and heat source(wood burner)HAPS lb/mmBtu, (Hardwood) 36 Natural Gas start up burner(1 MMBtu/hr) G-25 1-4, 1-5 5 Ink and painting operations G-27 ES 14,ES 17 20 Woodwaste Transfer(Rechipper) system NES-13-25HP NONE NONE ES-13-40HP NONE NONE ES—13—CC NONE NONE ES-13—PO NONE NONE ES-13—PS NONE NONE ES03—CC NONE NONE ES03—CS NONE NONE ES03—PSS NONE NONE ES03—SMS-1 21 Dry Waste transfer system ES03—SMS-2 NONE NONE ES03—SS NONE NONE ESO4 12 wood sander ES 12 17 dry wood residual storage silo 10 glue mixing,application and hot ES 13—GMO presses operations(Hardwood) 28 glue mixing,application and hot presses operations,(softwood) ES 16 9 plywood hog ES20 18 JVat Operations: Heating of Blocks ES21 33 JEnd Sealer Spray Booth 4 ES22 34 Tongue and Groove Saw I=1 2 Bark hogging operations: Hammer hog.truck dump-no controls - h 1 'f I 12 24 Dry Waste truck dump I=2 .. . 3 Core.chipping and handling operations 1-3 4 Green veneer hogging operations .. I-- 6 6 Plywood surface patching 1-7 .. . 7 Maintenance parts washer k � 1-8. 8 Veneer diverter exhaust cyclone,., .. 11 2.50 horsepower diesel-fired water IES-19 pump. . 250 HP Diesel Fired Water Pump _ r 35 42—IES23 Y IES-23 37 250 HP Diesel-Fire ater Pump#2 IES—GWS 16 Green wood fuel storage silo. f F ^ , i 5. Appendix D AERO Emission Forms and Calculations COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit: 03424 Moncure,NC 27559 County : Chatham DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 1. Emission Source ID(from permit)or Group GR2 consisting of I-10, 1-9 Emission Source Group ID 2. Emission Source Description: Green Veneer Stackers 3. Operating Scenario ID/Description: OS —32/Green Veneer Stackers 4. SCC Number/Description: 30700799/Plywood Operations ;Other Not Classified 5. Throughput/units in 2016: 155347 TON/yr (e.g. production or fuel use): 6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content Btu/units 7. Capture Efficiency (%of Emissions from this Process Vented to Control Device or Stack): 8. Control Device Information :None Order CS—ID CD ID Control Device Description as listed inpermit) 9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines): ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description (in feet) Circle(enter#): (F) (Feet/sec) (Acfm) Rectangle(L x W) in 0.1 feet) FEP-Fug4 FUGITIVE(NO 1 72 Area= 1 Stackers STACK 6 10C VERTICAL STACK 66 1 340 150 7068.58 Veneer dryer er IOcool VERTICAL STACK 46 4 105 35 26389.37 Veneer dryer er 10coolA VERTICAL STACK 46 4 105 35 26389.37 Veneer dryer ern r I r � F y 9 Operating Scenario: OS-26 Emission Source/Group ID: G-24 r-• i 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016) Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 ) 11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359 � I 12. Seasonal Periods Percent Annual Throu h ut: an-Feb +Dec 25% March-May 25% une-Aug. 25% Sept.-Nov. 25% 016 1 �016 �016 016 13. Actual Emissions per Pollutant Listed Attach calculations and documentation of emission factors or other estimation methods used. Emissions- Emission Control r GHG CAS GHG Estimation Efficiency Emission Ef Control Pollutants Pollutants Method Code (Net after Factor Tons/Year See Instructions all controls 2016 ' i Criteria Emissions- Emission Control Pollutant Criteria Estimation Efficiency Emission (NAA Code Pollutants Method Code (Net after Factor Ef Control Pollutants (Tons/Year) (See Instructions) all controls) 2016 CO CO 12.55 04 0 0.0006 AFTER NOx NOx 08 0 TSP TSP 08 65 PM10 PM10 08 65 Iry 1 PM2.5 PM2.5 08 65 S02 S02 08 0 VOC VOC 37.03 04 0 0.00177 AFTER Emission Control HAP/TAP CAS Emissions Estimation Efficient Emission Pollutants (In Alphabetical HAP/TAPS y EF Control Order) (see instructions) (Pounds/Year) Method Code (Net after all Factor -� f See Instructions controls)) ° 2016 Acetaldehyde 75-07-0 1004.28 08 0 0.000024 AFTER i Acrolein 107-02-8 284.546 08 0 0.0000068 AFTER aS -J Benzene 71-43-2 146.4575 08 0 0.0000035 AFTER Cumene 98-82-8 698.8115 08 0 0.0000167 AFTER Ethyl chloride chloroethane 75-00-3 18.78841 08 0 4.49E-7 AFTER Ethylene dichloride 107-06-2 28.78936 08 0 6.88E-7 AFTER 1 2-dichloroethane Formaldehyde 50-00-0 1046.125 04 0 0.000025 AFTER Methanol 67-56-1 1728.1985 08 0 0.0000413 AFTER Methyl bromide 74-83-9 27.57585 08 0 6.59E-7 AFTER Methylene chloride 75-09-2 24.7304 08 0 5.91E-7 AFTER (( Phenol 108-95-2 142.69145 08 0 0.00000341 AFTER Trichlorobenzene 12,4- 120-82-1 52.7247 08 0 0.00000126 AFTER 10 Vinyl chloride 75-01-4 18.16073 08 0 4.34E-7 AFTER Vin lidene chloride 75-35-4 26.48789 08 0 6.33E-7 AFTER X lene 1330-20-7 78.25015 08 0 0.00000187 AFTER - i i 3 1 i 'r 11 ) COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit: 03424 Moncure,NC 27559 County : Chatham DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 1. Emission Source ID(from permit)or Group G-24 consisting of ES01—A,ESO1—B,ES09,ES10 Emission Source Group ID 2. Emission Source Description: Veneer dryers and heat source(wood burner) 3. Operating Scenario ID/Description: OS—27Neneer dryers and heat source(wood burner)HAPS lb/mmBtu, (Softwood) 4. SCC Number/Description: 30700740/Plywood Operations ; Direct Wood—Fired Dryer:Non—specified Pine Species Veneer 5. Throughput/units in 2016: 107912 E6BTU/yr (e.g.production or fuel use): 6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content Btu/units 7. Capture Efficiency (%of Emissions from this Process Vented to Control 100 Device or Stack): 8. Control Device Information Order CS—ID CD ID Control Device Description as listed inpermit) 1 CS-1 CD02 Multic clone 720 six—inch diameter tubes 9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines): ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description (in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm) Rectangle(L x W) in 0.1 feet) 09A VERTICAL STACK 66 1 350 155 7304.2 Veneer dryer er 09B VERTICAL STACK 66 1 370 100 4712.38 Veneer dryer erp 09C VERTICAL STACK 66 1 340 150 7068.58 Veneer dryer er 09cool VERTICAL STACK 46 4 107 35 26389.37 Veneer d er e 09coolA IVERTICAL STACK 46 4 107 35 26389.37 Veneer dryer erp 10A VERTICAL STACK 66 1 350 1 155 7304.2 Veneer dryer erp 12 r Hydrogen chloride (hydrochloric acid Lead Unlisted Compounds (Specify and Component of PBC—Other 1.66184 08 0 0.0000154 AFTER PBC) Manganese Unlisted Compounds(Specify MNC—Other 268.70088 08 0 0.00249 AFTER Component of MNC Mercury,vapor(Component 7439-97-6 0.1241 08 0 0.00000115 AFTER of HGC Methyl chloride 74-87-3 2.87046 08 0 0.0000266 AFTER -p Methyl ethyl ketone 78-93-3 0.58165 08 0 0.00000539 AFTER Methyl isobutyl ketone 108-10-1 48.02084 08 0 0.000445 AFTER Naphthalene(Component of 91-20-3 0.87732 08 0 0.00000813 AFTER h . POMT Nickel metal(Component of 7440-02-0 1.26257 08 0 0.0000117 AFTER NIC Phosphorus Metal,Yellow 7723-14-0 588.1204 08 0 0.00545 AFTER or White Polycyclic Organic Matter yl (Inc PAH,dioxins,etc.NC POM 2.40644 08 0 0.0000223 AFTER AP 42 historic amorphous lob Pro ionaldeh de 123-38-6 2.30932 08 0 0.0000214 AFTER i 15 COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit : 03424 Moncure,NC 27559 County : Chatham DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 1. Emission Source ID(from permit) or Group G-24 consisting of ESO1—A, ESO1—B, ES09, ES10 Emission Source Group ID 2. Emission Source Description: Veneer dryers and heat source(wood burner) 3. Operating Scenario ID/Description: OS —30/Veneer dryers and heat source(wood burner) lbs/SF, (Hardwood) 4. SCC Number/Description: 30700734/Plywood Operations ; Hardwood Plywood, Veneer Dryer Direct Wood—fired, Heated Zones 5. Throughput/units in 2016: 113581000 FT2/yr (e.g. production or fuel use): 6. Fuel Information (If fuel is used) % Sulfur %Ash Heat Content Btu/units 7. Capture Efficiency (%of Emissions from this Process Vented to Control 100 Device or Stack): 8. Control Device Information Order CS—ID CD ID Control Device Description as listed inpermit) I CS-1 CD02 Multic clone 720 six—inch diameter tubes 9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines): ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description (in feet) Circle(enter#): (F) (Feet/sec) Rate(Aefm) Rectangle(L x W) (in 0.1 feet) 09A VERTICAL STACK 66 1 350 155 7304.2 Veneer dryer er 09B VERTICAL STACK 66 1 370 100 4712.38 Veneer dryer err) 09C VERTICAL STACK 66 1 340 150 7068.58 Veneer dryer er 09cool VERTICAL STACK 46 4 107 35 26389.37 Veneer dryer er 09coolA I VERTICAL STACK 46 4 107 35 26389.37 Veneer dr er er 10 IVERTICAL STACK 66 1 350 155 7304.2 Veneer dryer er 1013 IVERTICAL STACK 1 66 1 370 100 4712.38 Veneer dr er ern 16 IOC VERTICAL STACK 66 1 340 150 7068.58 Veneer dryer er 10cool VERTICAL STACK 46 4 105 35 26389.37 Veneer dryer erp 10coolA VERTICAL STACK 46 4 105 35 26399-37 Veneer dryer er � 1 C ' F 17 r� i Operating Scenario: OS-30 Emission Source/Group ID: G-24 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016) Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 ) 11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359 12. Seasonal Periods Percent Annual Throu h ut: an-Feb +Dec 250�o March-May 25% une-Aug. 25o/a �01 ept.-Nov. 25"�0 -' 016 �016 �016 6 13. Actual Emissions per Pollutant Listed Attach calculations and documentation of emission factors or other estimation methods used. Emissions- Emission Control GHG GHG Estimation Efficiency Emission Pollutants CAS Pollutants Method Code (Net after Factor Ef Control Tons/Year See Instructions all controls 2016 Criteria Emissions- Emission Control Pollutant Criteria Estimation Efficiency Emission (NAAant Code Pollutants Method Code y Ef Control - Pollutants (Net after Factor 1 ? (Tons/Year) (See Instructions) all controls) 2016 CO CO 21.35 04 0 0.000376 AFTER NOx NOx 08 0 TSP TSP 08 65 PM10 PM10 08 65 1 PM2.5 PM2.5 08 65 S02 S02 08 0 VOC VOC 7.61 04 0 0.000134 AFTER Emission Control G HAP/TAP CAS Emissions Estimation Efficiency Emission Pollutants (In Alphabetical HAP/TAPS clency EF Control (see instructions) Method Code (Net after all Factor j { Order) (Pounds/Year) See Instructions controls) ` 2016 ` Acetaldehyde 75-07-0 594.02863 08 0 0.00000523 AFTER Benzene 71-43-2 32.93849 08 0 2.9E-7 AFTER L Cumene 98-82-8 1014.27833 08 0 0.00000893 AFTER Ethyl chloride 75-00-3 27.25944 08 0 2.4E-7 AFTER chloroethane Ethylene dichloride 107-06-2 41.79781 08 0 3.68E-7 AFTER 1,2-dichloroethane Formaldehyde 50-00-0 1116.50123 04 0 0.00000983 AFTER Methanol 67-56-1 1077.88369 08 0 0.00000949 AFTER Methyl bromide 74-83-9 40.09409 08 0 3.53E-7 AFTER Methyl ethyl ketone 78-93-3 114.71681 08 0 0.00000101 AFTER Methyl isobutyI ketone 108-10-1 109.3785 08 0 9.63E-7 AFTER 'Il Methylene chloride 75-09-2 35.8916 08 0 3.16E-7 AFTER Phenol 1 108-95-2 185.13703 08 0 0.00000163 AFTER ,I _; 18 i I Pro ionaldeh de 123-38-6 103.13155 08 0 9.08E-7 AFTER Trichlorobenzene 12 4— 120-82-1 76.66718 08 0 6.75E-7 AFTER 4 Vinyl chloride 75-01-4 26.35079 08 0 2.32E-7 AFTER Vin lidene chloride 75-35-4 40.88916 08 0 3.6E-7 AFTER X lene 1330-20-7 44.8645 08 0 3.95E-7 AFTER x �, .. y t j 19 COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit: 03424 Moncure,NC 27559 County : Chatham DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 1. Emission Source ID(from permit)or Group G-24 consisting ofES01—A,ESO1—B,ES09,ES10 Emission Source Group ID 2. Emission Source Description: Veneer dryers and heat source(wood burner) 3. Operating Scenario ID/Description: OS—31/Veneer dryers and heat source(wood burner)HAPS lb/mmBtu, (Hardwood) 4. SCC Number/Description: 30700740/Plywood Operations ;Direct Wood—Fired Dryer: Non—specified Pine Species Veneer 5. Throughput/units in 2016: 292908 E6BTU/yr (e.g. production or fuel use): 6. Fuel Information (If fuel is used) rSulfur %Ash Heat Content Btu/units 7. Capture Efficiency (%of Emissions from this Process Vented to Control 100 Device or Stack): 8. Control Device Information Order CS—ID CD ID Control Device Description as listed inpermit) I CS-1 CD02 Multic clone 720 six—inch diameter tubes 9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines): ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description (in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm) Rectangle(L x W) in 0.1 feet) 09A VERTICAL STACK 66 1 350 155 7304.2 Veneer dryer erp 09B VERTICAL STACK 66 1 370 100 4712.38 Veneer dryer erp 09C VERTICAL STACK 66 1 340 150 7068.58 Veneer dryer erp 09coo1 VERTICAL STACK 46 4 107 35 26389.37 Veneer d er le09cooIA VERTICAL STACK 46 4 107 35 26389.37 Veneer d er 10A VERTICAL STACK 66 1 350 155 7304.2 Veneer d er 20 IOB VERTICAL STACK 66 1 370 100 4712.38 Veneer dryer er IOC VERTICAL STACK 66 1 340 150 7068.58 Veneer dryer er IOcool VERTICAL STACK 46 4 105 35 26389.37 Veneer dryer er lOcoolA VERTICAL STACK 46 4 105 35 26389.37 Veneer dryer er 4 I i 4 f h I I i 21 j ` Operating Scenario: OS—31 Emission Source/Group ID: G-24 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016) Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 ) 11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359 12. Seasonal Periods Percent Annual Throu h ut: an—Feb +Dec March--May une—Au Set Nov. 016 25% �016 25% 016 g. 25% 016 25% 13. Actual Emissions per Pollutant Listed Attach calculations and documentation of emission factors or other estimation methods used. Emissions— Emission Control G GHG CAS y GHG Estimation Efficient Emission Pollutants Pollutants Method Code (Net after Factor Ef Control Tons/Year See Instructions all controls 2016 Criteria Emissions— Emission Control ` NAA S Pollutant Criteria Estimation Efficiency Emission ( Q ) Code Pollutants Method Code Ef Control lltt Pollutants (Net after Factor (Tons/Year) (See Instructions) all controls) 2016 CO CO 08 0 NOx NOx 29.73 08 0 0.203 AFTER TSP TSP 24.73 08 65 AFTER PM10 PM10 24.73 08 65 AFTER PM2.5 PM2.5 24.24 08 65 AFTER S02 S02 0.47 08 0 0.00318 AFTER VOC VOC 08 0 HAP/TAP Emissions Emission Control CAS Estimation Efficient Emission Pollutants (In Alphabetical HAP/TAPS y EF Control Order) (see instructions) (pounds/Year) Method Code (Net after all Factor li See Instructions controls) - 2016 Acrolein 107-02-8 37.19932 08 0 0.000127 AFTER Arsenic Unlisted Compounds(Specify ASC—Other 0.94316 08 0 0.00000322 AFTER Component of ASC Cadmium Metal(elemental unreacted, Component of 7440-43-9 1.39424 08 0 0.00000476 AFTER CDC Carbon tetrachloride 56-23-5 0.74692 08 0 0.00000255 AFTER Chlorine 7782-50-5 231.39732 08 0 0.00079 AFTER Chromic acid(VI) (Component of So1CR6 7738-94-5 2.04157 08 0 0.00000697 AFTER CRC Chromium Unlisted Compounds(Specify CRC—Other 7..02979 08 0 0.000024 AFTER Component of CRC 22 I L Hydrogen chloride 7647-01-0 101.34617 08 0 0.000346 AFTER (hydrochloric acid Lead Unlisted Compounds 2 (Specify and Component of PBC—Other 4.51078 08 0 0.0000154 AFTER PBC) - tl Manganese Unlisted j Compounds(Specify MNC—Other 729.34092 08 0 0.00249 AFTER Component of MNC Mercury,vapor(Component 7439-97-6 0.33684 08 0 0.00000115 AFTER .S of HGC Methyl chloride 74-87-3 7.79135 08 0 0.0000266 AFTER Naphthalene(Component of 91-20-3 2.38134 08 0 0.00000813 AFTER POMT Nickel metal(Component of 7440-02-0 3.42702 08 0 0.0000117 AFTER NIC Phosphorus Metal,Yellow 7723-14-0 1596.3486 08 0 0.00545 AFTER or White Polycyclic Organic Matter (Inc PAH, dioxins,etc.NC POM 6.53185 08 0 0.0000223 AFTER AP 42 historic amorphous lob i l r' I 23 COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID • 1900039 306 Corinth Road Permit : 03424 Moncure, NC 27559 County : Chatham DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 1. Emission Source ID(from permit)or Group G-24 consisting of ESO1—A, ESO1—B, ES09, ES 10 Emission Source Group ID 2. Emission Source Description: Veneer dryers and heat source (wood burner) 3. Operating Scenario ID/Description: OS —36/Natural Gas start up burner(1 MMBtu/hr) 4. SCC Number/Description: 30701399/Paper—Miscellaneous Processes ; Other Not Classified 5. Throughput/units in 2016: 0.004 E6FT3S/yr (e.g. production or fuel use): 6. Fuel Information (1f fuel is used) %Sulfur %Ash Heat Content Btu/units 7. Capture Efficiency (%of Emissions from this Process Vented to Control 100 Device or Stack): 8. Control Device Information Order CS—ID CD ID Control Device Description as listed inpermit) 1 CS-1 CD02 Multic clone 720 six—inch diameter tubes 9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines): ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description (in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm) Rectangle(L x W) in 0.1 feet) 09A VERTICAL STACK 66 1 350 155 7304.2 Veneer dryer er 09B VERTICAL STACK 66 1 370 100 4712.38 Veneer dryer er 09C VERTICAL STACK 66 1 340 150 7068.58 Veneer dryer er 09cool VERTICAL STACK 46 4 107 35 26389.37 Veneer dryer er 09cooIA VERTICAL STACK 46 4 107 35 26389.37 Veneer dryer er 10A VERTICAL STACK 66 1 350 155 7304.2 Veneer dryer er 1013 VERTICAL STACK 66 1 370 100 1 4712.38 Veneer dryer er 1 OC VERTICAL STACK 66 1 1 340 150 1 7068.58 Veneer dryer er 24 r� 10cool VERTICAL STACK 46 4 105 35 26389.37 Veneer drver ern 10coolA IVERTICAL STACK 1 46 1 4 105 35 26389.37 Veneer dryer er 25 r-� i r Operating Scenario: OS—36 Emission Source/Group ID: G-24 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016) Hours per Day ( 1 ) Days per Week ( 1 ) Weeks per Year ( 52 ) 11.Typical Start& End Times For Operating Scenario: Start: 0 End: 2359 I _ 12. Seasonal Periods Percent Annual Throu h ut: an—Feb +Dec o March—May o une—Aug. o Sept.—Nov. o 016 25/0 016 25/0 016 25/0 016 25/o 13. Actual Emissions per Pollutant Listed Attach calculations and documentation of emission factors or other estimation methods used. Emissions— Emission Control GHG CAS GHG Estimation Efficiency Emission Ef Control Pollutants Pollutants Method Code (Net after Factor Tons/Year See Instructions all controls 2016 'h Criteria Emissions— Emission Control Pollutant Criteria Estimation Efficiency Emission ` (NAA Code Pollutants Method Code (Net afterFactor Ef Control Pollutants i (Tons/Year) (See Instructions) all controls) 2016 CO CO 0 08 0 NOx NOx 0 08 0 TSP TSP 0 08 65 PM10 PM10 0 08 65 PM2.5 PM2.5 0 08 65 —' S02 S02 0 08 0 VOC VOC 0 08 0 HAP/TAP CAS Emissions Estimation Emission Control Efficiency Pollutants (In Alphabetical HAP/TAPS y Emission EF Control Order) (see instructions) (Pounds/Year) Method Code (Net after all Factor See Instructions controls) �- 2016 Arsenic Unlisted { Compounds(Specify ASC—Other 7.3E-8 08 0 u Component of ASC Benzene 71-43-2 0.00000766 08 0 Cadmium Unlisted Compounds(Specify CDC—Other 4.01E-7 08 0 Component of CDC Chromium Unlisted — Compounds (Specify CRC—Other 5.11E-7 08 0 Component of CRC Formaldehyde 50-00-0 0.000274 08 0 Lead Unlisted Compounds (Specify and Component of PBC—Other 1.82E-7 08 0 PBC MNC—Other 1.39E-7 08 0 26 Manganese Unlisted Compounds(Specify Component of MNC Mercury,vapor(Component 7439-97-6 9.48E-7 08 0 of HGC i Naphthalene(Component of 91-20-3 0.00000223 08 0 POMT Nickel Unlisted Compounds NIC—Other 7.66E-7 08 0 (Specify Component of NIC Polycyclic Organic Matter (Inc PAH,dioxins,etc.NC pOM 3.22E-7 08 0 AP 42 historic amorphous lob i � j i i 27 COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit: 03424 Moncure,NC 27559 County : Chatham DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 1. Emission Source ID(from permit)or Group G-25 consisting of 1-4. 1-5 Emission Source Group ID 2. Emission Source Description: Ink and painting operations 3. Operating Scenario ID/Description: OS—5/Ink and painting operations 4. SCC Number/Description: 40500597/Printing—General ;Other Not Classified 5. Throughput/units in 2016: 175 GAL/yr (e.g. production or fuel use): 6. Fuel Information (If fuel is used) /o Sulfur ro Ash Heat Content Btu/units 7. Capture Efficiency (%of Emissions from this Process Vented to Control Device or Stack): 8. Control Device Information :None Order CS—ID CD ID Control Device Description as listed inpermit) 9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines): ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description (in feet) Circle(enter#): (F) (Feet/sec) (Acfm) Rectangle(L x W) (in 0.1 feet) EP—FUG FUGITIVE(NO 1 72 Area— 1 ERP for Fugitive STACK) sources 28 Operating Scenario: OS—5 Emission Source/Group ID: G-25 �I 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016) Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 ) s 11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359 12. Seasonal Periods Percent Annual Throu h ut: an—Feb +Dec 25% arch—May 25"�o une—Aug. 25"�o �016 ept.—Nov. 25% _1 016 016 016 13. Actual Emissions per Pollutant Listed Attach calculations and documentation of emission factors or other estimation methods used. j Emissions— Emission Control GHG CAS GHG Estimation Efficiency Emission Ef Control Pollutants Pollutants Method Code (Net after Factor Tons/Year See Instructions all controls 2016 Criteria Emissions— Emission Control (NAAQS) Pollutant Criteria Estimation Efficiency Emission Ef Control Pollutants Code Pollutants Method Code (Net after Factor (Tons/Year) (See Instructions) all controls) 2016 CO CO 08 NOx NOx 08 TSP TSP 08 PM10 PM10 08 PM2.5 PM2.5 08 � S02 S02 08 VOC VOC 0.14 03 Emission HAP/TAP Emissions Control CAS Estimation Emission EF Control Pollutants (In HAP/TAPS Efficiency (see instructions) Method Code Factor - Alphabetical Order) (Pounds/Year) (Net after all controls) See Instructions 2016 ' r ' r ' i i i 29 COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit : 03424 Moncure,NC 27559 County : Chatham DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 1. Emission Source ID(from permit)or Group G-27 consisting of ES 14, ES 17 Emission Source Group ID 2. Emission Source Description: Woodwaste Transfer system 3. Operating Scenario ID/Description: OS—20/Woodwaste Transfer(Rechipper) system 4. SCC Number/Description: 30700799/Plywood Operations ; Other Not Classified 5. Throughput/units in 2016: 23134 TON/yr (e.g. production or fuel use): 6. Fuel Information (If fuel is used) %Sulfur %Ash Heat Content Btu/units 7. Capture Efficiency (%of Emissions from this Process Vented to Control 100 Device or Stack): 8. Control Device Information Order CS—ID CD ID Control Device Description as listed inpermit) 1 CS-12 CD18 Cyclone 60 inches in diameter 2 CS-12 CD03—WWTC Woodwaste transfer cyclone 154 inches in diameter 3 CS-12 CD06 Ba filter(7,095 square feet of filter area 9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines): ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description (in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm) Rectangle(L x W) (in 0.1 feet) erp for dry waste erp-08 VERTICAL STACK 51 3.5 80 55 31749.72 transfer cyclone and ba filter 30 j Operating Scenario: OS —20 Emission Source/Group ID: G-27 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016) Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 ) 11.Typical Start& End Times For Operating Scenario: Start: 0 End: 2359 12. Seasonal Periods Percent Annual Throu h ut: an—Feb +Dec 25% March—May 25% une—Aug. 25% Sept.—Nov. 25% 016 I 016 016 I 016 � 13. Actual Emissions per Pollutant Listed : } Attach calculations and documentation of emission factors or other estimation methods used. Emissions— Emission Control _ GHG CAS GHG Estimation Efficiency Emission Ef Control Pollutants Pollutants Method Code (Net after Factor Tons/Year See Instructions all controls 2016 11 Emissions— Emission Control Criteria Pollutant Criteria Estimation Efficiency Emission (NAAQS) Code Pollutants Method Code (Net afterFactor Ef Control Pollutants (Tons/Year) (See Instructions) all controls) 2016 CO CO 08 0 NOx NOx 08 0 TSP TSP 0.28 08 99.7 0.024 AFTER PM10 PM10 0.13 08 99.7 0.011 AFTER PM2.5 PM2.5 0.05 08 99.7 0.0046 AFTER S02 S02 08 0 VOC VOC 08 0 HAP/TAP CAS Emissions Emission Estimation Control Emission - � Pollutants (In HAP/TAPS Efficiency EF Control (see instructions) Method Code Factor Alphabetical Order) (Pounds/Year) See Instructions) (Net after all controls) 2016 -j ,I f 31 COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit : 03424 Moncure,NC 27559 County : Chatham DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 1. Emission Source ID(from permit)or ES03—SMS-1 Emission Source Group ID 2. Emission Source Description: Woodworking operations consisting of three string machine saws, a core saw, a strip saw, a panel sawing system and a core composer, saw, sander baghouse (ID No. CD-05) 3. Operating Scenario ID/Description: OS —21/Dry Waste transfer system 4. SCC Number/Description: 30700710/Plywood Operations ; Sawing 5. Throughput/units in 2016: 88938000 FT2/yr (e.g. production or fuel use): 6. Fuel Information (If fuel is used) %Sulfur %Ash Heat Content Btu/units 7. Capture Efficiency (%of Emissions from this Process Vented to Control 100 Device or Stack): 8. Control Device Information Order CS—ID CD ID Control Device Description as listed inpermit) 1 CS-3 CD03—WWTC Woodwaste transfer cyclone 154 inches in diameter 2 CS-3 CD06 Ba filter 7,095 square feet of filter area 9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines): ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description (in feet) Circle(enter#): (F) (Feet/sec) Rate(Aefm) Rectangle(L x W) (in 0.1 feet) erp for dry waste erp-08 VERTICAL STACK 51 3.5 80 55 31749.72 transfer cyclone and ba filter 32 i Operating Scenario: OS—21 Emission Source/Group ID: ES03—SMS-1 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016) Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 ) - 11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359 12. Seasonal Periods Percent Annual Throu h ut: an—Feb +Dec 25% arch—May 25° une—Aug. 25% Sept.—Nov. 25% 016 016 �° 016 016 13. Actual Emissions_per Pollutant Listed Attach calculations and documentation of emission factors or other estimation methods used. Emissions— Emission Control GHG CAS GHG Estimation Efficiency Emission Ef Control Pollutants Pollutants Method Code (Net after Factor Tons/Year See Instructions all controls 2016 Criteria Emissions— Emission Control Pollutant Criteria Estimation Efficiency Emission (NAA Code Pollutants Method Code (Net after Factor Ef Control Pollutants , � (Tons/Year) (See Instructions) all controls) 2016 CO CO 08 0 NOx NOx 08 0 TSP TSP 14.22 04 85 AFTER PM10 PM10 14.22 04 85 AFTER PM2.5 PM2.5 14.22 04 0 AFTER S02 S02 08 0 VOC VOC 08 0 HAP/TAP Emissions Emission Control CAS Estimation Emission Pollutants (In HAP/TAPS Efficiency EF Control (see instructions) Method Code Factor Alphabetical Order) (Pounds/Year) See Instructions) (Net after all controls) 2016 33 COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit : 03424 Moncure,NC 27559 County : Chatham DAQ Region : PRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 1. Emission Source ID(from permit)or ESO4 Emission Source Group ID 2. Emission Source Description: wood sander 3. Operating Scenario ID/Description: OS — 12/wood sander 4. SCC Number/Description: 30700702/Plywood Operations ; Sanding Operations 5. Throughput/units in 2016: 20320000 FT2/yr (e.g. production or fuel use): 6. Fuel Information (If fuel is used) %Sulfur %Ash Heat Content Btu/units 7. Capture Efficiency (%of Emissions from this Process Vented to Control 100 Device or Stack): 8. Control Device Information Order CS—ID CD ID Control Device Description as listed inpermit) 1 CS-10 CD05 Ba filter 6,200 square feet of filter area 2 CS-10 CD03—WWTC Woodwaste transfer cyclone 154 inches in diameter 3 CS-10 CD06 Ba filter 7,095 square feet of filter area 9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines): ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP (in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm) Description Rectangle(L x W) (in 0.1 feet) EP—WS DOWNWARD—FACING VENT 10 1 72 1 47.12 ERP for wood sander 34 �J Operating Scenario: OS— 12 Emission Source/Group ID: ESO4 i 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016) Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 ) l 11. Typical Start& End Times For Operating Scenario: Start: 0 End: 2359 12. Seasonal Periods Percent Annual Throu h ut: an—Feb +Dec 25% ch—May 250�o une—Aug. 25"�u Sept.—Nov. 25%016 �ar 16 016 016 13. Actual Emissions per Pollutant Listed : I Attach calculations and documentation of emission factors or other estimation methods used. J Emissions— Emission Control GHG CAS GHG Estimation Efficiency Emission Ef Control Pollutants Pollutants Method Code (Net after Factor (Ton ear) See Instructions all controls 2016 Emissions— Emission Control Criteria Pollutant Criteria Estimation Efficient Emission Ef Control Pollutants y (NAA Code Pollutants Method Code (Net after Factor , (Tons/Year) (See Instructions) all controls) 2016 CO CO 08 0 NOx NOx 08 0 TSP TSP 0.12 04 95 AFTER -" PM10 PM10 0.12 04 95 AFTER PM2.5 PM2.5 0.12 04 95 AFTER S02 S02 08 0 VOC VOC 1.54 08 0 AFTER HAP/TAP Emissions Emission Control Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission EF Control Alphabetical Order) (Pounds/Year) (see instructions) Method Code (Net after all Factor ' I See Instructions controls) 2016 Acetaldehyde 75-07-0 35.97 08 0 Formaldehyde 50-00-0 24.79 08 0 Methanol 67-56-1 157.07 08 0 i 35 COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit : 03424 Moncure,NC 27559 County : Chatham DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 1. Emission Source ID(from permit) or ES12 Emission Source Group ID 2. Emission Source Description: dry wood residual storage silo that receives material from the dry wood residual system cyclone ES03 3. Operating Scenario ID/Description: OS— 17/dry wood residual storage silo 4. SCC Number/Description: 30700799/Plywood Operations ; Other Not Classified 5. Throughput/units in 2016: 88938000 FT2/yr (e.g. production or fuel use): 6. Fuel Information (If fuel is used) %Sulfur %Ash Heat Content Btu/units 7. Capture Efficiency (%of Emissions from this Process Vented to Control 100 Device or Stack): 8. Control Device Information Order CS—ID CD ID Control Device Description as listed inpermit) 1 CS-5 CD21 Cartridge filter 1,800 square feet of filter area 9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines): ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description (in feet) Circle(enter#): (F) (Feet/sec) Rate (Acfm) Rectangle(L x W) (in 0.1 feet) e —12 IVERTICALSTACK 60 1 0.7 72 0.45 10.39 silo er 36 i � Operating Scenario: OS— 17 Emission Source/Group ID: ES12 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016) i Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 ) 11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359 12. Seasonal Periods Percent Annual Throu h ut: ron, —Feb +Dec 25a�o �March—Mayune—Au . TSept.—Nov.. 6 16 25% 016 g 25% 6 25% 13. Actual Emissions per Pollutant Listed : } Attach calculations and documentation of emission factors or other estimation methods used. i Emissions— Emission Control GHG CAS GHG Estimation Efficiency Emission Ef Control Pollutants Pollutants Method Code (Net after Factor TonsNear See Instructions all controls 2016 Criteria Emissions— Emission Control (NAAQS) Pollutant Criteria Estimation Efficiency Emission Ef Control Pollutants Code Pollutants Method Code (Net after Factor (Tons/Year) (See Instructions) all controls) 2016 CO CO 08 0 NOx NOx 08 0 TSP TSP 0.41 10 99.9 0.00000929 AFTER t PM10 PM10 0.41 10 99.9 0.00000929 AFTER PM2.5 PM2.5 0.41 10 99.9 0.00000929 AFTER i" S02 S02 08 0 VOC VOC 08 0 HAP/TAP Emissions Emission Control Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission EF Control Alphabetical Order) (see instructions) (Pounds/Ye Method Code (Net after all Factor ar) See Instructions controls) 2016 1 37 COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit: 03424 Moncure,NC 27559 County : Chatham DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 1. Emission Source ID(from permit)or ES 13—GMO Emission Source Group ID 2. Emission Source Description: glue mixing,application and hot press operations, including curtain coater, plywood spreader, 25 press and 40 press and paper overlay operation 3. Operating Scenario ID/Description: OS— 10/glue mixing,application and hot presses operations(Hardwood) 4. SCC Number/Description: 30700780/Plywood Operations ;Plywood Press: Phenol—formaldehyde Resin 5. Throughput/units in 2016: 46653000 FT2/yr (e.g. production or fuel use): 6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content Btu/units 7. Capture Efficiency (%of Emissions from this Process Vented to Control Device or Stack): 8. Control Device Information :None Order CS—ID CD ID Control Device Description as listed inpermit) i I i - 9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines): ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description (in feet) Circle(enter#): (F) (Feet/sec) (Acfm) Rectangle(L x W) in 0.1 feet) FUGITIVE(NO erp for gluing and erp-13 STACK 3.05 125 Area = press operations 38 ' I Operating Scenario: OS— 10 Emission Source/Group ID: ES13—GMO i 10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016) Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 ) 11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359 12. Seasonal Periods Percent Annual Throu h ut: an—Feb +Dec 250�o arch—May 25"�o une—Aug. 25"�u �016 ept.—Nov. 25% 016 016 016 L - 13. Actual Emissions per Pollutant Listed Attach calculations and documentation of emission factors or other estimation methods used. Emissions— Emission Control GHG CAS GHG Estimation Efficiency Emission Ef Control Pollutants Pollutants Method Code (Net after Factor (Ton ear) See Instructions all controls 2016 Criteria Emissions— Emission Control (NAAQS) Pollutant Criteria Estimation Efficiency Emission Ef Control Pollutants Code Pollutants Method Code (Net after Factor (Tons/Year) (See Instructions) all controls) 2016 CO CO 08 NOx NOx 08 TSP TSP 4.67 08 0.0002 PM10 PM10 4.67 08 0.0002 PM2.5 PM2.5 1.94 08 0.0000832 S02 S02 08 VOC VOC 3.99 08 0.000171 - HAP/TAP Emissions Emission Control Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission EF Control (see instructions) Method Code (Net after all Factor Alphabetical Order) (Pounds/Year) See Instructions controls) 2016 Formaldehyde 50-00-0 233.265 08 0.000005 Methanol 67-56-1 5178.483 08 0.000111 Phenol 108-95-2 741.7827 08 0.0000159 39 COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit : 03424 Moncure,NC 27559 County : Chatham DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 1. Emission Source ID(from permit)or ES13—GMO Emission Source Group ID 2. Emission Source Description: glue mixing, application and hot press operations, including curtain coater, plywood spreader, 25 press and 40 press and paper overlay operation 3. Operating Scenario ID/Description: OS—28/glue mixing, application and hot presses operations, (softwood) 4. SCC Number/Description: 30700799/Plywood Operations ; Other Not Classified 5. Throughput/units in 2016: 42285000 FT2/yr (e.g. production or fuel use): 6. Fuel Information (If fuel is used) %Sulfur %Ash Heat Content Btu/units 7. Capture Efficiency (°io of Emissions from this Process Vented to Control Device or Stack): 8. Control Device Information :None Order CS—ID CD ID Control Device Description as listed inpermit) I i - 1 9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines): ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description (in feet) Circle(enter#): (F) (Feet/sec) (Acfm) Rectangle(L x W) (in 0.1 feet) F rp-13 FUGITIVE(NO 3.05 125 Area= erp for gluing and STACK press operations 40 —i Operating Scenario: OS-28 Emission Source/Group ID: ES 13-GMO 10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016) Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 ) 11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359 j 12. Seasonal Periods Percent Annual Throu h ut:ran--Feb +Dec o arch-May o une-Aug. 250�o Sept.-Nov. 25% 6 25�O 016 25�° 016 016 13. Actual Emissions per Pollutant Listed Attach calculations and documentation of emission factors or other estimation methods used. Emissions- Emission Control GHG CAS GHG Estimation Efficiency Emission Ef Control Pollutants Pollutants Method Code (Net after Factor -! Tons/Year See Instructions all controls 2016 Criteria Emissions- Emission Control 1 (NAAQS) Pollutant Criteria Estimation Efficiency Emission Ef Control Pollutants Code Pollutants Method Code (Net after Factor (Tons/Year) (See Instructions) all controls) 2016 -� CO CO 08 NOx NOx 08 TSP TSP 4.23 08 0.0002 PM10 PM10 4.23 08 0.0002 PM2.5 PM2.5 1.76 08 0.0000832 S02 S02 08 VOC VOC 12.41 08 0.000587 HAP/TAP Emissions Emission Control CAS Estimation Efficiency Emission Pollutants (In (see instructions) HAP/TAPS Method Code (Net after all Factor EF Control Alphabetical Order) (Pounds/Year) See Instructions controls) 2016 Acetaldehyde 75-07-0 152.64885 08 0.00000361 Formaldehyde 50-00-0 211.425 08 0.000005 Methanol 67-56-1 4693.635 08 0.000111 Methyl ethyl ketone 78-93-3 34.33542 08 8.12E-7 Methyl isobutyl 108-10-1 34.54684 08 8.17E-7 ketone Phenol 108-95-2 114.59235 08 0.00000271 i 41 COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit : 03424 Moncure, NC 27559 County : Chatham DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 1. Emission Source ID(from permit) or ES 16 Emission Source Group ID 2. Emission Source Description: Plywood waste hog 3. Operating Scenario ID/Description: OS —9/plywood hog 4. SCC Number/Description: 30700710/Plywood Operations ; Sawing 5. Throughput/units in 2016: 13578 TON/yr (e.g. production or fuel use): 6. Fuel Information (If fuel is used) %Sulfur %Ash Heat Content Btu/units 7. Capture Efficiency (%of Emissions from this Process Vented to Control 100 Device or Stack): 8. Control Device Information Order CS—ID CD ID Control Device Description as listed inpermit) 1 CS-3 CD03—WWTC Woodwaste transfer cyclone 154 inches in diameter 2 CS-3 CD06 Ba filter 7,095 square feet of filter area 9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines): ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description (in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm) Rectangle(L x W) (in 0.1 feet) erp for dry waste erp-08 VERTICAL STACK 51 3.5 80 55 31749.72 transfer cyclone and ba filter 42 I Operating Scenario: OS—9 Emission Source/Group ID: ES16 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016) Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 ) 11.Typical Start& End Times For Operating Scenario: Start: 0 End: 2359 12. Seasonal Periods Percent Annual Throu h ut: - an—Feb +Dec o March—May o une—Aug. o Sept.—Nov. 25% 016 25/0 016 25/0 016 25/0 016 13. Actual Emissions per Pollutant Listed Attach calculations and documentation of emission factors or other estimation methods used. Emissions— Emission Control _ GHG CAS GHG Estimation Efficiency Emission Ef Control Pollutants Pollutants Method Code (Net after Factor Tons/Ye See Instructions all controls 2016 i Criteria Emissions— Emission Control (NAAQS) Pollutant Criteria Estimation Efficiency Emission Ef Control Pollutants Code Pollutants Method Code (Net after Factor (Tons/Year) (See Instructions) all controls) 2016 CO CO 08 0 NOx NOx 08 0 TSP TSP 0.16 08 99.9 0.024 AFTER PM10 PM10 0.07 08 99.9 0.011 AFTER PM2.5 PM2.5 0.03 08 99.9 0.0046 AFTER S02 S02 08 0 VOC VOC 08 0 HAP/TAP Emissions Emission Control Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission EF Control (see instructions) Method Code Factor Alphabetical Order) (Pounds/Year) (Net after all controls) See Instructions 2016 I 43 i E U s r� uJI i r✓l .� LE �t`}f L .tl i tys_ 1: t�)tr, -'+� ii _r Facility.Name: .MoricurePlywood .,. Facility ID 1900039 306 Corinth Road:: Permit.: :03424 ... . ... ... .. Moncure,NC 27559 County Chatham Q Region :RRO r. North:Carolina Department of Environment and Natural Resources. Division of Air.Quality Air.Pollutant Point Source Emissions Inventor Calendar Year 2016. . 1...Emission Source ID.(from permit)or ES20 Emission Source Group ID 2. Emission Source Description: vat Operations 3. Operating Scenario;ID/Description: . OS— 18/Vat Operations: Heating of Blocks. 4. SCC Ni mber/Description; : . 39999997/,N4iscellaneous Industrial.Processes ;:Other Not Classified 5. Throughput/units in 2016' 82800000. FT2/yr (e.g.prodpe.on or fuel use 6.: Fuel Information (:If fuel is used) 16/01 0 Sulfur /o:Ash Heat Content Btu%units a_ 7. Captdre E:ff ciency (%of Emissions from this Process Vented to Control bpvice or Stack): 8. ontrol Device Information :None Order CS—ID. .: . CD ID .. .:. Control Device Description as listed in ermrt F. 9.Emission Release Point ERP Information: Sources vented to more than one ERP.use additional entry lines ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate : :ERP:Descriptioat. in feet Circle enter#: Feet/sec Acfra Rectangle(L x:W) .. (in 0.1.feet) FUGITIVE:(NO 2 ERP 0 . . 1 100 Area= 1 :-. Vats :STACK i 44 Operating Scenario: OS— 18 Emission Source/Group ID: ES20 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016) Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 ) 11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359 j 12. Seasonal Periods Percent Annual Throu h ut:ran--Feb +Dec 25% 25% une—Aug. 25% ept.—Nov. 25%6 �arch—May 16 �016 016 13. Actual Emissions per Pollutant Listed : Attach calculations and documentation of emission factors or other estimation methods used. Emissions— Emission Control _ GHG CAS GHG Estimation Efficiency Emission Pollutants Pollutants Method Code (Net after Factor Ef Control Tons/Year See Instructions all controls 2016 Criteria Emissions— Emission Control (NAAQS) Pollutant Criteria Estimation Efficiency Emission Ef Control Pollutants Code Pollutants Method Code (Net after Factor (Tons/Year) (See Instructions) all controls) i f 2016 CO CO 08 NOx NOx 08 TSP TSP 08 PM10 PM10 08 PM2.5 PM2.5 08 c S02 S02 08 VOC VOC 1.81 08 Emission Control HAP/TAP Emissions CAS HAP/TAPS Estimation Efficiency Emission Pollutants (In (see instructions) Method Code (Net after all Factor EF Control Alphabetical Order) (Pounds/Year) See Instructions controls) 2016 Acetaldehyde 75-07-0 386.676 08 0.00000467 Methanol 67-56-1 607.752 08 0.00000734 45 COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit : 03424 Moncure,NC 27559 County : Chatham DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 1. Emission Source ID(from permit)or ES20 Emission Source Group ID 2. Emission Source Description: vat Operations 3. Operating Scenario ID/Description: OS— 18/Vat Operations: Heating of Blocks 4. SCC Number/Description: 39999997/Miscellaneous Industrial Processes ;Other Not Classified 5. Throughput/units in 2016: 82800000 FT2/yr (e.g. production or fuel use): 6. Fuel Information (If fuel is used) % Sulfur %Ash Heat Content Btu/units 7. Capture Efficiency (%of Emissions from this Process Vented to Control Device or Stack): 8. Control Device Information :None Order CS—ID CD ID Control Device Description as listed inpermit) 9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines): ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description (in feet) Circle(enter#): (F) (Feet/sec) (Acfm) Rectangle(L x W) in 0.1 feet) ERP-20 FUGITIVE(NO 1 STACK) 100 Area= 1 Vats 44 �I t Operating Scenario: OS— 18 Emission Source/Group ID: ES20 y 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016) Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 ) 11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359 12. Seasonal Periods Percent Annual Throu h ut: F —Feb +Dec I 25% arch—May 25% 016 25% Sept.—Nov. 25% i 016 016 016 13. Actual Emissions per Pollutant Listed Attach calculations and documentation of emission factors or other estimation methods used. Emissions— Emission Control GHG CAS GHG Estimation Efficiency Emission Ef Control Pollutants Pollutants Method Code (Net after Factor Tons/Year See Instructions all controls 2016 Emissions— Emission Control Criteria Pollutant Criteria Estimation Efficiency Emission Ef Control (NAAQS) Code Pollutants Method Code (Net after Factor Pollutants (Tons/Year) (See Instructions) all controls) 2016 - CO CO 08 NOx NOx 08 TSP TSP 08 PM10 PM10 08 ' PM2.5 PM2.5 08 S02 S02 08 VOC VOC 1.81 08 — HAP/TAP Emissions Emission Control Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission EF Control Alphabetical Order) (see instructions) (Pounds/Year) Method Code (Net after all Factor See Instructions controls) 2016 Acetaldehyde 75-07-0 386.676 08 0.00000467 Methanol 67-56-1 607.752 08 0.00000734 45 COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AFRO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit : 03424 Moncure,NC 27559 County : Chatham DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 1. Emission Source ID(from permit) or ES21 Emission Source Group ID 2. Emission Source Description: End sealer spray booth 3. Operating Scenario ID/Description: OS—33/End Sealer Spray Booth 4. SCC Number/Description: 40202108/Flatwood Products Coating ; Sealer 5. Throughput/units in 2016: 540 GAL/yr (e.g. production or fuel use): 6. Fuel Information (If fuel is used) %Sulfur %Ash Heat Content Btu/units 7. Capture Efficiency (%of Emissions from this Process Vented to Control Deice or Stack): 8. Control Device Information :None Order CS—ID CD ID Control Device Description as listed inpermit) i __j 9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional entrylines): ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description (in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm) Rectangle(L x W) (in 0.1 feet) EP-21 VERTICAL STACK 20 1 70 10 471.23 End Sealer Spray Booth 46 Emission Source/Group ID: ES21 Operating Scenario: OS 33 P 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016) Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 ) 11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359 12. Seasonal Periods Percent Annual Throu h ut: w ran--Feb +Dec 25% arch—May 250�o une—Aug. 25"�o �016 ept.—Nov. 25%6 016 �016 13. Actual Emissions per Pollutant Listed Attach calculations and documentation of emission factors or other estimation methods used. Emissions— Emission Control r_ GHG CAS GHG Estimation Efficiency Emission Ef Control Pollutants Pollutants Method Code (Net after Factor Tons/Ye See Instructions all controls 2016 Criteria Emissions— Emission Control AA S Pollutant Criteria Estimation Efficiency Emission Q ) Ef Control Code Pollutants Method Code (Net after Factor Pollutants (Tons/Year) (See Instructions) all controls) 2016 CO CO 08 NOx NOx 08 TSP TSP 0.01 03 PM10 PM10 0.01 03 PM2.5 PM2.5 08 S02 S02 08 VOC VOC 0.01 03 HAP/TAP Emissions Emission Control Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission EF Control (see instructions) Method Code Factor Alphabetical Order) (Pounds/Year) (Net after all controls) r, { See Instructions 2016 X tl 47 COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit : 03424 Moncure,NC 27559 County : Chatham DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 1. Emission Source ID (from permit)or ES22 Emission Source Group ID 2. Emission Source Description: Tongue and groove saw (plywood finishing) 3. Operating Scenario ID/Description: OS —34/Tongue and Groove Saw 4. SCC Number/Description: 30700710/Plywood Operations ; Sawing 5. Throughput/units in 2016: 354000 FT2/yr (e.g. production or fuel use): 6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content Btu/units 7. Capture Efficiency (%of Emissions from this Process Vented to Control 100 Device or Stack): 8. Control Device Information Order CS—ID CD ID Control Device Description as listed inpermit) 1 CS-7 C1306 Ba filter 7,095 square feet of filter area 9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines): ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description (in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm) Rectangle(L x W) (in 0.1 feet) y erp-06 VERTICAL STACK 30 2.8 72 50 18472.56 erp for woodwaste system 48 Operating Scenario: OS—34 Emission Source/Group ID: ES22 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016) Hours per Day ( 3 ) Days per Week ( 1 ) Weeks per Year ( 35 ) 11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359 12. Seasonal Periods Percent Annual Throu h ut: r011an--Feb +Dec 25% March—May une—Aug. 25% Sept.—Nov. 25% 016 25% 016 016 13. Actual Emissions per Pollutant Listed Attach calculations and documentation of emission factors or other estimation methods used. Emissions— Emission Control GHG CAS GHG Estimation Efficiency Emission Ef Control ~ Pollutants Pollutants Method Code (Net after Factor (Tons ear) See Instructions all controls 2016 r, Emissions— Emission Control Criteria Pollutant Criteria Estimation Efficiency Emission (NAA Code Pollutants Method Code (Net after Factor Ef Control Pollutants (Tons/Year) (See Instructions) all controls) {" 2016 CO CO 08 0 w NOx NOa 08 0 TSP TSP 0.01 02 99.5 PM10 PM10 0 02 99.5 PM2.5 PM2.5 0 08 99.5 S02 S02 08 0 VOC VOC 0.01 08 0 0.0000755 AFTER HAP/TAP Emissions Emission Control CAS Estimation Efficiency Emission EF Control Pollutants de(in (see instructions) HAP/TAPS Method Code (Net after all Factor Alphabetical Order (Pounds/I'ear P ) ) See Instructions controls) r 2016 Acetaldehyde 75-07-0 0.19789 08 0 5.59E-7 AFTER Formaldehyde 50-00-0 0.13771 08 0 3.89E-7 AFTER Methanol 67-56-1 2.41428 08 0 0.00000682 AFTER M 49 COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit : 03424 Moncure,NC 27559 County : Chatham DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 1. Emission Source ID(from permit)or I-1 Emission Source Group ID 2. Emission Source Description: Bark hogging operations with two saws 3. Operating Scenario ID/Description: OS —2/Bark hogging operations 4. SCC Number/Description: 30700799/Plywood Operations ; Other Not Classified 5. Throughput/units in 2016: 19128 TON/yr (e.g. production or fuel use): 6. Fuel Information (If fuel is used) %Sulfur %Ash Heat Content Btu/units 7. Capture Efficiency (%of Emissions from this Process Vented to Control Device or Stack): 8. Control Device Information :None Order CS—ID CD ID Control Device Description as listed inpermit) 9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional entrylines): ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description (in feet) Circle(enter#): (F) (Feet/sec) (Acfm) Rectangle(L x W) (in 0.1 feet) EP—FUG FUGITIVE (NO 1 72 Area— 1 ERP for Fugitive STACK) sources 50 Operating Scenario: OS 2 Emission Source/Group ID: 1-1 10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016) Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 ) 11.Typical Start& End Times For Operating Scenario: Start: 0 End: 2359 12. Seasonal Periods Percent Annual Throu h ut: ri —Feb +Dec 25% March—May 25% une—Aug. 25% �016 ept.—Nov. 25% 016 016 13. Actual Emissions per Pollutant Listed Attach calculations and documentation of emission factors or other estimation methods used. Emissions— Emission Control GHG CAS GHG Estimation Efficiency Emission Ef Control Pollutants Pollutants Method Code (Net after Factor Tons/Year See Instructions all controls 2016 Emissions— Emission Control Criteria Pollutant Criteria Estimation Efficiency Emission (NAAQS) Ef Control Pollutants Code Pollutants Method Code (Net after Factor (Tons/Year) (See Instructions) all controls) 2016 CO CO 08 NOx NOx 08 TSP TSP 0.01 08 PM10 PM10 0.01 08 PM2.5 PM2.5 0 08 S02 S02 08 VOC VOC 08 HAP/TAP Emissions Emission Control Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission EF Control (see instructions) Method Code Factor Alphabetical Order) (Pounds/Year) See Instructions) (Net after all controls) 2016 51 COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit : 03424 Moncure,NC 27559 County : Chatham DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 1. Emission Source ID(from permit)or I—1 1 Emission Source Group ID 2. Emission Source Description: hammer hog truck dump 3. Operating Scenario ID/Description: OS—25/Hammer hog truck dump—no controls 4. SCC Number/Description: 30704004/Wood Bulk Handling and Storage—Wood/Bark; Loading 5. Throughput/units in 2016: 1517 TON/yr (e.g. production or fuel use): 6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content Btu/units 7. Capture Efficiency (%of Emissions from this Process Vented to Control Device or Stack): 8. Control Device Information :None Order CS—ID CD ID Control Device Description as listed inpermit) 9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional entrylines): ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description (in feet) Circle(enter#): (F) (Feet/sec) (Acfm) Rectangle(L x W) (in 0.1 feet) EP—Fug3 FUGITIVE(NO 1 72 Area— 1 Hammer Hog Truck STACK) Dump 52 Operating Scenario: OS—25 Emission Source/Group ID: I-11 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016) Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 ) 11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359 12. Seasonal Periods Percent Annual Throu h ut: an—Feb +Dec 25°�° ° une—Aug. ° �016 ept.—Nov. 25% 016 �arch—May 16 25%O �016 25%° 13. Actual Emissions per Pollutant Listed Attach calculations and documentation of emission factors or other estimation methods used. Emissions— Emission Control Q GHG CAS GHG Estimation Efficiency Emission Ef Control Pollutants Pollutants Method Code (Net after Factor Tons/Year See Instructions all controls 2016 Emissions— Emission Control Criteria Pollutant Criteria Estimation Efficiency Emission (NAAQS) Code Pollutants Method Code (Net after Factor Ef Control Pollutants (Tons/Year) (See Instructions) all controls) ' 2016 CO CO 08 NOx NOx 08 TSP TSP 0 08 PM10 PM10 0 08 PM2.5 PM2.5 0 08 r S02 S02 08 VOC VOC 08 HAP/TAP Emissions Emission Control Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission (see instructions) Method Code Factor EF Control Alphabetical Order) (Pounds/Year) (Net after all controls) See Instructions 2016 I � 53 COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit : 03424 Moncure,NC 27559 County : Chatham DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 1. Emission Source ID(from permit)or I-12 Emission Source Group ID 2. Emission Source Description: dry waste truck dump 3. Operating Scenario ID/Description: OS —24/Dry Waste truck dump 4. SCC Number/Description: 30704004/Wood Bulk Handling and Storage—Wood/Bark ; Loading 5. Throughput/units in 2016: 1243 TON/yr (e.g. production or fuel use): 6. Fuel Information (If fuel is used) % Sulfur %Ash Heat Content Btu/units 7. Capture Efficiency (%of Emissions from this Process Vented to Control Device or Stack): 8. Control Device Information :None Order CS—ID CD ID Control Device Description as listed inpermit) 9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines): ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description (in feet) Circle(enter#): (F) (Feet/sec) (Acfm) Rectangle(L x W) (in 0.1 feet) EP—Fug2 FUGITIVE(NO 1 72 Area— 1 Dry Waste Truck STACK) Dump 54 Operating Scenario: OS—24 Emission Source/Group ID: 1-12 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016) Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 ) 11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359 r' 12. Seasonal Periods Percent Annual Throu h ut: an—Feb +Dec ° ° une—Aug. ° �016 ept.—Nov. i 016 25/° �arch—Nlay 16 25/° �016 25/° 25% 13. Actual Emissions per Pollutant Listed : Attach calculations and documentation of emission factors or other estimation methods used. Emissions— Emission Control GHG GHG Estimation Efficiency Emission Pollutants CAS Pollutants Method Code (Net after Factor Ef Control Tons/Year See Instructions all controls 2016 Criteria Emissions— Emission Control (NAAQS) Pollutant Criteria Estimation Efficiency Emission Ef Control Pollutants Code Pollutants Method Code (Net after Factor (Tons/Year) (See Instructions) all controls) 2016 CO CO 08 NOx NOx 08 TSP TSP 0 08 PM10 PM10 0 08 PM2.5 PM2.5 0 08 S02 S02 08 VOC VOC 08 Emission HAP/TAP CAS Emissions Estimation Control Emission EF Control Pollutants (In HAP/TAPS Efficiency Factor(see instructions) Method Code Alphabetical Order) (Pounds/Year) See Instructions) (Net after all controls) 2016 I I . 55 COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit : 03424 Moncure,NC 27559 County : Chatham DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 1. Emission Source ID(from permit)or I-2 Emission Source Group ID 2. Emission Source Description: Core chipping and handling 3. Operating Scenario ID/Description: OS —3/Core chipping and handling operations 4. SCC Number/Description: 30700799/Plywood Operations ; Other Not Classified 5. Throughput/units in 2016: 58 TON/yr (e.g. production or fuel use): 6. Fuel Information (If fuel is used) % Sulfur %Ash Heat Content Btu/units 7. Capture Efficiency (%of Emissions from this Process Vented to Control Device or Stack): 8. Control Device Information :None Order CS—ID CD ID Control Device Description as listed inpermit) 9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines): ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description (in feet) Circle(enter#): (F) (Feet/sec) (Acfm) Rectangle(L x W) in 0.1 feet) EP—FUG FUGITIVE (NO 1 72 Area— I ERP for Fugitive STACK) sources 56 I, Operating Scenario: OS—4 Emission Source/Group ID: I-3 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016) Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 ) 11.Typical Start& End Times For Operating Scenario: Start: 0 End: 2359 12. Seasonal Periods Percent Annual Throu h ut: une An—Feb +Dec rch—May ept.—Nov.25% 25% 01 25% 016 25% 6 �016 6 13. Actual Emissions per Pollutant Listed : Attach calculations and documentation of emission factors or other estimation methods used. Emissions— Emission Control GHG CAS GHG Estimation Efficiency Emission Ef Control Pollutants Pollutants Method Code (Net after Factor Tons/Ye See Instructions all controls 2016 Criteria Emissions— Emission Control Pollutant Criteria Estimation Efficiency Emission (NAA Code Pollutants Method Code (Net after Factor Ef Control Pollutants ` (Tons/Year) (See Instructions) all controls) 2016 CO CO 08 NOx NOx 08 TSP TSP 0.01 08 PM10 PM10 0.01 08 PM2.5 PM2.5 0 08 S02 S02 08 VOC VOC 08 HAP/TAP Emissions Emission Control Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission EF Control (see instructions) Method Code Factor Alphabetical Order) (Pounds/Year) See In (Net after all controls) structions 2016 59 COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit : 03424 Moncure,NC 27559 County : Chatham DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 1. Emission Source ID(from permit) or I-6 Emission Source Group ID 2. Emission Source Description: Plywood surface patching 3. Operating Scenario ID/Description: OS —6/Plywood surface patching 4. SCC Number/Description: 30700799/Plywood Operations ; Other Not Classified 5. Throughput/units in 2016: 3960 GAL/yr (e.g. production or fuel use): 6. Fuel Information (If fuel is used) %Sulfur %Ash Heat Content Btu/units 7. Capture Efficiency (%of Emissions from this Process Vented to Control Device or Stack): 8. Control Device Information :None Order CS—ID CD ID Control Device Description as listed inpermit) i i i i 1 9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines): ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description (in feet) Circle(enter#): (F) (Feet/sec) (Acfm) Rectangle(L x W) in 0.1 feet) EP—FUG FUGITIVE (NO 1 72 TArea— 1 ERP for Fugitive STACK sources 60 i Operating Scenario: OS—6 Emission Source/Group ID: I-6 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016) Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 ) 11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359 12. Seasonal Periods Percent Annual Throu h ut: ran—Feb +Dec March—May ° 25%une—Aug. Sept.—Nov. 25% 016 25% 016 25�° 016 016 - 13. Actual Emissions per Pollutant Listed Attach calculations and documentation of emission factors or other estimation methods used. Emissions— Emission Control GHG CAS GHG Estimation Efficiency Emission Ef Control Pollutants Pollutants Method Code (Net after Factor Tons/Year See Instructions all controls 2016 Criteria Emissions— Emission Control Pollutant Criteria Estimation Efficient Emission (NAAQS) y Ef Control Pollutants Code Pollutants Method Code (Net after Factor (Tons/Year) (See Instructions) all controls) 2016 CO CO 08 NOx NOx 08 TSP TSP 08 PM10 PM10 08 PM2.5 PM2.5 08 S02 S02 08 VOC VOC 0.08 03 HAP/TAP CAS Emissions Emission Estimation Control Emission Pollutants (In HAP/TAPS Efficiency EF Control (see instructions) Method Code Factor Alphabetical Order) (Pounds/Year) See Instructions) (Net after all controls) 2016 1, 61 COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit : 03424 Moncure, NC 27559 County : Chatham DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 1. Emission Source ID(from permit)or I-7 Emission Source Group ID 2. Emission Source Description: Maintenance parts washers 3. Operating Scenario ID/Description: OS —7/Maintenance parts washer 4. SCC Number/Description: 40202105/Flatwood Products Coating ; Equipment Cleanup 5. Throughput/units in 2016: (e.g. production or fuel use): 6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content Btu/units 7. Capture Efficiency (%of Emissions from this Process Vented to Control Device or Stack): 8. Control Device Information :None Order CS—ID CD ID Control Device Description as listed inpermit) 9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines): ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description (in feet) Circle(enter#): (F) (Feet/sec) (Acfm) Rectangle(L x W) (in 0.1 feet) EP—FUG FUGITIVE (NO 1 72 Area— 1 ERP for Fugitive STACK) sources 62 c, Operating Scenario: OS —7 Emission Source/Group ID: I-7 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016) Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 ) 11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359 12. Seasonal Periods Percent Annual Throu h ut: ran--Feb +Dec 25% rch—May 25"�u une—Aug. 25% �016 ept.—Nov. 25% 6 �01.6 �016 13. Actual Emissions per Pollutant Listed : Attach calculations and documentation of emission factors or other estimation methods used. Emissions— Emission Control GHG CAS GHG Estimation Efficiency Emission Ef Control Pollutants Pollutants Method Code (Net after Factor Tons/Year See Instructions all controls 2016 Criteria Emissions— Emission Control Pollutant Criteria Estimation Efficiency Emission (NAAQS) Code Pollutants Method Code (Net after Factor Ef Control Pollutants (Tons/Year) (See Instructions) all controls) 2016 CO CO 08 NOx NOx 08 TSP TSP 08 PM10 PM10 08 PM2.5 PM2.5 08 S02 S02 08 VOC VOC 08 HAP/TAP CAS Emissions Emission Estimation Control Emission Pollutants (In HAP/TAPS Efficiency EF Control (see instructions) Method Code Alphabetical Order) (Pounds/Year) (Net after all controls) Factor See Instructions 2016 63 COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit : 03424 Moncure,NC 27559 County : Chatham DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 1. Emission Source ID(from permit) or I-8 Emission Source Group ID 2. Emission Source Description: Veneer diverter exhaust cyclone 3. Operating Scenario ID/Description: OS —8/Veneer diverter exhaust cyclone 4. SCC Number/Description: 30700799/Plywood Operations ; Other Not Classified 5. Throughput/units in 2016: 155347 TON/yr (e.g. production or fuel use): 6. Fuel Information (1f fuel is used) /o Sulfur %Ash Heat Content Btu/units 7. Capture Efficiency (%of Emissions from this Process Vented to Control Device or Stack): 8. Control Device Information :None Order CS—ID CD ID Control Device Description as listed inpermit) I i — 1 9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines): ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description (in feet) Circle(enter#): (F) (Feet/sec) (Acfm) Rectangle(L x W) (in 0.1 feet) [EP—FUG FUGITIVE (NO 1 72 Area— I ERP for Fugitive STACK) sources 64 a Operating Scenario: OS—8 Emission Source/Group ID: I-8 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016) Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 ) 11.Typical Start& End Times For Operating Scenario: Start: 0 End: 2359 12. Seasonal Periods Percent Annual Throu h ut: ran--Feb +Dec o arch—May une—Aug. 25% Sept.—Nov. 25% 6 25�O 016 25% 016 016 13. Actual Emissions per Pollutant Listed Attach calculations and documentation of emission factors or other estimation methods used. Emissions— Emission Control _ GHG CAS GHG Estimation Efficiency Emission Ef Control Pollutants Pollutants Method Code (Net after Factor Tons/Ye See Instructions all controls 2016 Criteria Emissions— Emission Control Pollutant Criteria Estimation EfficiencyEmission (NAAQS) Ef Control Pollutants Code Pollutants Method Code (Net after Factor (Tons/Year) (See Instructions) all controls) 2016 CO CO 08 NOx NOx 08 TSP TSP 0.54 02 PM10 PM10 0.54 02 PM2.5 PM2.5 08 SO2 SO2 08 VOC VOC 08 HAP/TAP Emissions Emission Control Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission EF Control (see instructions) Method Code Factor Alphabetical Order) (Pounds/Year) See Instructions) (Net after all controls) 2016 N 65 COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit : 03424 Moncure,NC 27559 County : Chatham DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 1. Emission Source ID(from permit)or IES-19 Emission Source Group ID 2. Emission Source Description: Diesel—fired water pump (250 Horsepower maximum power output) for emergency purposes only 3. Operating Scenario ID/Description: OS — 11/250 horsepower diesel—fired water pump 4. SCC Number/Description: 20200407/Diesel ; Exhaust 5. Throughput/units in 2016: 52.8 E6BTU/yr (e.g. production or fuel use): 6. Fuel Information (If fuel is used) %Sulfur 0.002 %Ash Heat Content 133332 Btu/gallon Btu/units 7. Capture Efficiency (%of Emissions from this Process Vented to Control Device or Stack): 8. Control Device Information :None Order CS—ID CD ID Control Device Description as listed inpermit) 9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines): ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description (in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm) Rectangle(L x W) (in 0.1 feet) erp—wp VERTICAL STACK 8 0.42 72 1 8.31 erp for diesel—fired water pump 66 Operating Scenario: OS- 11 Emission Source/Group ID: IES-19 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016) Hours per Day ( 3 ) Days per Week ( 1 ) Weeks per Year ( 44 ) 11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359 12. Seasonal Periods Percent Annual Throu h ut:an ' Feb +Dec 25% March-May 25% une-Aug. 25% rOl NoV. 25% 16 016 016 13. Actual Emissions per Pollutant Listed : Attach calculations and documentation of emission factors or other estimation methods used. Emissions- Emission Control _ GHG CAS GHG Estimation Efficiency Emission Ef Control Pollutants Pollutants Method Code (Net after Factor Tons/Year See Instructions all controls 2016 Criteria Emissions- Emission Control (NAAQS) Pollutant Criteria Estimation Efficiency Emission Ef Control Pollutants Code Pollutants Method Code (Net after Factor (Tons/Year) (See Instructions) all controls) 2016 CO CO 0.03 08 0.95 NOx NOx 0.12 08 4.41 TSP TSP 0.01 08 0.31 PM10 PM10 0.01 08 0.31 PM2.5 PM2.5 0.01 08 0.31 S02 S02 0.01 08 0.29 VOC VOC 0.01 08 0.35 Emissions Emission Control HAP/TAP CAS Estimation Efficiency Emission EF Control Alphabetical Order) (see instructions) Pollutants (In AI HAP/TAPS P (Pounds/Year) Method Code (Net after all Factor See Instructions controls) 2016 Acetaldehyde 75-07-0 0.0405 08 0.000767 Acrolein 107-02-8 0.00488 08 0.0000925 Benzene 71-43-2 0.04926 08 0.000933 Formaldehyde 50-00-0 0.0623 08 0.00118 Naphthalene(Component of 91-20-3 0.00448 08 0.0000848 POMT Polycyclic Organic Matter (Inc PAH,dioxins,etc.NC POM 0.00887 08 0.000168 AP 42 historic amorphous lob X lene 1330-20-7 0.01505 08 0.000285 67 COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit : 03424 Moncure,NC 27559 County : Chatham DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 1. Emission Source ID(from permit)or IES-19 Emission Source Group ID 2. Emission Source Description: Diesel—fired water pump(250 Horsepower maximum power output) for emergency purposes only 3. Operating Scenario ID/Description: OS —35/250 HP Diesel Fired Water Pump#2—IES23 4. SCC Number/Description: 20200401/Diesel ; Diesel 5. Throughput/units in 2016: (e.g. production or fuel use): 6. Fuel Information (1f fuel is used) % Sulfur %Ash Heat Content Btu/units 7. Capture Efficiency (%of Emissions from this Process Vented to Control Device or Stack): 8. Control Device Information :None Order CS—ID CD ID Control Device Description as listed inpermit) �__l I i 1 9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines): ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description (in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm) Rectangle(L x W) in 0.1 feet) erp—wp VERTICAL STACK 8 0.42 72 1 8.31 erp for diesel—fired water pump 69 Operating Scenario: OS—35 Emission Source/Group ID: IES-19 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016) Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 ) 11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359 12. Seasonal Periods Percent Annual Throu h ut: an—Feb +Dec o M o une—Aug. o �016 ept.—Nov. o 016 25/0 �arch— ay 16 25/0 �016 25/0 13. Actual Emissions per Pollutant Listed Attach calculations and documentation of emission factors or other estimation methods used. Emissions— Emission Control GHG CAS GHG Estimation Efficiency Emission Ef Control Pollutants Pollutants Method Code (Net after Factor Tons/Ye See Instructions all controls 2016 Criteria Emissions— Emission Control (NAAQS) Pollutant Criteria Estimation Efficiency Emission Ef Control Pollutants Code Pollutants Method Code (Net after Factor (Tons/Year) (See Instructions) all controls) 2016 CO CO 08 NOx NOx 08 TSP TSP 08 PM10 PM10 08 PM2.5 PM2.5 08 S02 S02 08 VOC VOC 08 HAP/TAP Emissions Emission Control Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission (see instructions) Method Code Factor EF Control Alphabetical Order) (Pounds/Year) (Net after all controls) See Instructions 2016 — 70 COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit: 03424 Moncure,NC 27559 County : Chatham DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 1. Emission Source ID(from permit) or IES-23 Emission Source Group ID 2. Emission Source Description: Diesel—fired fire pump emergency engine(250 Horsepower maximum power output)for emergency purposes only[Area Source MACT ZZZZ,NSPS Subpart IIII] 3. Operating Scenario ID/Description: OS—37/250 HP Diesel—Fired Water Pump#2 4. SCC Number/Description: 20200401/Diesel ;Diesel 5. Throughput/units in 2016: 10.2 E6BTU/yr (e.g. production or fuel use): 6. Fuel Information (If fuel is used) /o Sulfur 0.002 /o Ash Heat Content 133332 Btu/gallon Btu/units 7. Capture Efficiency (%of Emissions from this Process Vented to Control Device or Stack): 8. Control Device Information :None Order CS—ID CD ID Control Device Description as listed inpermit) 9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines): ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description (in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm) Rectangle(L x W) in 0.1 feet) erp—wp VERTICAL STACK 8 0.42 72 1 8.31 erp for diesel—fired water pump 71 i Operating Scenario: OS—37 Emission Source/Group ID: IES-23 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016) Hours per Day ( 1 ) Days per Week ( 1 ) Weeks per Year ( 23 ) `- 11.Typical Start& End Times For Operating Scenario: Start: 0 End: 2359 12. Seasonal Periods Percent Annual Throu h ut: ran--Feb. +Dec 250�o 25"�o rune—�Aug. 25% Sept.—Nov. 25% 6 tarch—May 16 6 016 13. Actual Emissions per Pollutant Listed : Attach calculations and documentation of emission factors or other estimation methods used. Emissions— Emission Control GHG CAS GHG Estimation Efficiency Emission Ef Control Pollutants Pollutants Method Code (Net after Factor Tons/Year See Instructions all controls 2016 Criteria Emissions— Emission Control (NAAQS) Pollutant Criteria Estimation Efficiency Emission Ef Control Pollutants Code Pollutants Method Code (Net after Factor (Tons/Year) (See Instructions) all controls) 2016 - CO CO 0.01 08 NOx NOx 0.02 08 TSP TSP 08 PM10 PM10 08 PM2.5 PM2.5 08 S02 S02 08 VOC VOC 08 Emissions Emission Control HAP/TAP CAS HAP/TAPS Estimation Efficiency Emission EF Control Pollutants (In Alphabetical Order) (see instructions) (Pounds/Year) Method Code (Net after all Factor See Instructions controls) 2016 Acetaldehyde 75-07-0 0.008 08 Acrolein 107-02-8 0.001 08 Benzene 71-43-2 0.009 08 Formaldehyde 50-00-0 0.012 08 Naphthalene(Component of 91-20-3 0.001 08 POMT Polycyclic Organic Matter (Inc PAH,dioxins, etc.NC POM 0.002 08 AP 42 historic amorphous glob) - X lene 1330-20-7 0.003 08 r 72 COPY of RECORD Date Submitted: 6/14/2017 13:28:13 As entered in AERO Facility Name: Moncure Plywood Facility ID : 1900039 306 Corinth Road Permit : 03424 Moncure,NC 27559 County : Chatham DAQ Region : RRO North Carolina Department of Environment and Natural Resources Division of Air Quality Air Pollutant Point Source Emissions Inventory—Calendar Year 2016 1. Emission Source ID(from permit) or IES—GWS Emission Source Group ID 2. Emission Source Description: Green wood fuel storage silo 3. Operating Scenario ID/Description: OS — 16/Green wood fuel storage silo 4. SCC Number/Description: 30700799/Plywood Operations ; Other Not Classified 5. Throughput/units in 2016: 19128 TON/yr (e.g. production or fuel use): 6. Fuel Information (If fuel is used) %Sulfur %Ash Heat Content Btu/units 7. Capture Efficiency (%of Emissions from this Process Vented to Control Device or Stack): 8. Control Device Information :None Order CS—ID CD ID Control Device Description as listed inpermit) I i 9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines): ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description (in feet) Circle(enter#): (F) (Feet/sec) Rate(Aefm) Rectangle(L x W) (in 0.1 feet) e 11.1 DOWNWARD—FACING VENT 70 1.25 72 0.45 33.13 silo vent ep 11.2 DOWNWARD—FACING VENT 70 1.25 72 0.45 33.13 silo vent e l l.3 DOWNWARD—FACING VENT 70 1.25 72 0.45 33.13 silo vent e l l.4 DOWNWARD—FACING VENT 70 1.25 72 0.45 33.13 silo vent 74 Operating Scenario: OS— 16 Emission Source/Group ID: IES—GWS 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016) Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 ) 11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359 12. Seasonal Periods Percent Annual Throu h ut: Van—Feb +Dec 25% �March—May 25% une—Aug. 25% Sept.—Nov. 25% 16 16 016 016 - 13. Actual Emissions per Pollutant Listed Attach calculations and documentation of emission factors or other estimation methods used. Emissions— Emission Control GHG CAS GHG Estimation Efficiency Emission Ef Control Pollutants Pollutants Method Code (Net after Factor Tons/Ye See Instructions all controls 2016 Criteria Emissions— Emission Control (NAAQS) Pollutant Criteria Estimation Efficiency Emission Ef Control Pollutants Code Pollutants Method Code (Net after Factor (Tons/Year) (See Instructions) all controls) 2016 CO CO 08 NOx NOx 08 TSP TSP 0 08 PM10 PM10 0 08 PM2.5 PM2.5 0 08 S02 S02 08 VOC VOC 08 HAP/TAP Emissions Emission Control Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission EF Control (see instructions) Method Code Factor Alphabetical Order) (Pounds/Year) (Net after all controls) � See Instructions 2016 75 I Boise Cascade Wood Products-Moncure Plywood Emission Source(s): Fluidized Bed Wood Boiler and Two Direct Heated Dryers Source ID Number(s): ES-01,ES-09,ES-10,CD-02(multiclone on boiler) Emission Point(s): EP-09a-d,EP-10a-d 2016 Actual Process Throughput: 8,147 Boiler operating hours/yr 13,578 dry wood(ton/yr) 20,328 green wood(ton/yr) 400,819 MMBtu/yr Total Fuel Combusted 189,649 MMBtu/yr Green Wood Combusted 211,170 MMBtu/yr Dry Wood Combusted 113,581,000 sf/yr Hardwood Veneer Production 41,845,000 sf/yr Softwood Veneer Production 155,426,000 sf/yr Total Veneer Production 292,908 MMBtu/yr Btu of Wood Combusted-ratioed for Hardwood Veneer 107,912 MMBtu/yr Btu of Wood Combusted-ratioed for Softwood Veneer Actual Emissions Summary: Hardwood Softwood Total Emissions* Emissions* Emissions Compound Emission Factor Units Ref. Emission Factor Units Ref. ton/ r ton/ r ton/ r CO 3.76E-04 lb/sf 1 21.34 6.00E-04 Ib/sf 1 12.55 33.9 NOx 2.03E-01 lb/MMBtu 6 29.73 2.03E-01 lb/MMBtu 6 10.95 40.7 PM 8.308 lb/hr 3 24.73 8.308 lb/hr 3 9.11 33.8 PM10 8.308 lb/hr 3 24.73 8.308 lb/hr 3 9.11 33.8 PM2.5 8.14 lb/hr 3 24.24 8.14 lb/hr 3 8.93 33.2 VOC(as acetic acid-hardwood and pinene-softwood) 2.41E-04 lb/sf 1 13.70 1.07E-03 lb/sf 1 22.39 36.1 WPP1 VOC 1.34E-04 lb/sf 4 7.63 1.77E-03 Ib/sf 4 37.03 44.7 S02 3.18E-03 lb/MMBtu 6 0.47 3.18E-03 lb/MMBtu 6 0.17 0.64 Emissions* Emissions Emissions* Compound Emission Factor Units Ref. Ib/ r Emission Factor Units Ref. lb/ r Ib/ r Acetaldehyde(TH) 5.23E-06 Ib/sf 2 594.03 2.40E-05 Ib/sf 2 1004.28 1598.31 Aceto henone(H) 1.84E-06 lb/MMBtu 6 0.54 1.84E-06 lb/MMBtu 6 0.20 0.74 Acrolein TH 1.27E-04 lb/MMBtu 6 37.20 6.80E-06 lb/sf 2 284.55 321.75 Antimony&compounds H) 3.46E-06 lb/MMBtu 6 1.01 3.46E-06 lb/MMBtu 6 0.37 1.39 Arsenic&compounds (TH) 3.22E-06 lb/MMBtu 6 0.94 3.22E-06 lb/MMBtu 6 0.35 1.29 Benzene(TH) 2.90E-07 Ib/sf 2,5 32.97 3.50E-06 Ib/sf 2 146.46 179.42 Benzo(a) ene (T) 1.52E-08 lb/MMBtu 6 0.00 1.52E-08 lb/MMBtu 6 0.00 0.01 Beryllium&compounds TH 4.00E-08 lb/MMBtu 6 0.01 4.00E-08 lb/MMBtu 6 0.00 0.02 Cadmium&com ounds TH 4.76E-06 lb/MMBtu 6 1.39 4.76E-06 lb/MMBtu 6 0.51 1.91 Carbon tetrachloride TH 2.55E-06 Ib/MMBtu 6 0.75 2.55E-06 lb/MMBtu 6 0.28 1.02 Chlorine TH 7.90E-04 Ib/MMBtu 5 231.40 7.90E-04 lb/MMBtu 5 85.25 316.65 Chlorobenzene(TH) 1.66E-05 lb/MMBtu 6 4.86 1.66E-05 lb/MMBtu 6 1.79 6.65 Boise Cascade Wood Products-Moncure Plywood Emission Source(s): Fluidized Bed Wood Boiler and Two Direct Heated Dryers Source ID Number(s):ES-01,ES-09,ES-10,CD-02(multiclone on boiler) Emission Point(s): EP-09a-d,EP-10a-d 2016 Actual Process Throughput: 8,147 Boiler operating hours/yr 13,578 dry wood(ton/yr) 20,328 green wood(ton/yr) 400,819 MMBtu/yr Total Fuel Combusted 189,649 MMBtu/yr Green Wood Combusted 211,170 MMBtu/yr Dry Wood Combusted 113,581,000 sf/yr Hardwood Veneer Production 41,845,000 sf/yr Softwood Veneer Production 155,426,000 sf/yr Total Veneer Production 292,908 MMBtu/yr Btu of Wood Combusted-ratioed for Hardwood Veneer 107,912 MMBtu/yr Btu of Wood Combusted-ratioed for Softwood Veneer Actual Emissions Summary: Hardwood Softwood Total E Emissions* missions* Emissions* Compound Emission Factor Units Ref. Emissions* r Emission Factor Units Ref. Ib/ r Ib/ r Chloroform(TH) 2.55E-06 lb/MMBtu- 6 0.75 2.55E-06 lb/MMBtu 6 0.28 1.02 Chromium compounds H) 2.40E-05 lb/MMBtu 6 7.03 2.40E-05 lb/MMBtu 6 2.59 9.62 Chromium VI T/H) 6.97E-06 lb/MMBtu 6 2.04 6.97E-06 lb/MMBtu 6 0.75 2.79 Cobalt compounds(H) 2.12E-06 lb/MMBtu 6 0.62 2.12E-06 lb/MMBtu 6 0.23 0.85 Cumene(H) 8.93E-06 Ib/sf 2,5 1013. 11 1.67E-05 Ib/sf 2,5 698.81 1712.52 Dinitro henol,2,4-(H) 1.31E-07 lb/MMBtu 6 0.04 1.31E-07 lb/MMBtu 6 0.01 0.053 Di(2-eth lhex 1)phthalate DEHP)(TH) 4.65E-08 lb/MMBtu 6 0.01 4.65E-08 lb/MMBtu 6 0.01 0.019 Ethyl benzene H) 3.13E-05 lb/MMBtu 6 9.17 3.13E-05 lb/MMBtu 6 3.38 12.55 Ethyl chloride chloroethane)(H) 2.40E-07 lb/sf 2,5 27.23 4.49E-07 Ib/sf 2,5 18.78 46.01 Ethylene dichloride(1,2-dichloroethane)(TH) 3.68E-07 lb/sf 2,5 41.74 6.88E-07 Ib/sf 2,5 28.79 70.53 Formaldehyde(TH) 9.83E-06 lb/sf 1 1116.50 2.50E-05 lb/sf 1 1046.13 2162.63 Hexachlorodibenzo- -dioxin 1,2,3,6,7,8(T) 1.76E-11 lb/ODT 6 4.19E-07 1.76E-11 lb/ODT 6 4.19E-07 8.37E-07 Hydrogen chloride(hydrochloric acid)((TH) 3.46E-04 lb/MMBtu 6 101.35 3.46E-04 lb/MMBtu 6 37.34 138.68 Lead&compounds(H) 1.54E-05 lb/MMBtu 6 4.51 1.54E-05 lb/MMBtu 6 1.66 6.17 Manganese&compounds TH 2.49E-03 lb/MMBtu 6 729.34 2.49E-03 lb/MMBtu 6 268.70 998.04 Mercury,vapor(Include in Mercu &Com ds)(TH 1.15E-06 lb/MMBtu 6 0.34 1.15E-06 lb/MMBtu 6 0.12 0.46 Methanol(H) 9.49E-06 lb/sf 2 1077.88 4.13E-05 Ib/sf 2 1728.20 2806.08 Methyl bromide(H)(bromomethane) 3.53E-07 Ib/sf 2,5 40.07 6.59E-07 Ib/sf 2,5 27.57 67.63 Methyl chloride H)(chloromethane) 2.66E-05 lb/MMBtu 6 7.79 2.66E-05 lb/MMBtu 6 2.87 10.66 Methyl chlorofo (TH) 1,1,1trichloroethane) 3.93E-05 lb/MMBtu 6 11.51 3.93E-05 lb/MMBtu 6 4.24 15.75 Methyl ethyl ketone(TH) 1.01E-06 Ib/sf 2,5 114.43 5.39E-06 lb/MMBtu 6 0.58 115.01 Methyl isobutyl ketone(TH) 9.63E-07 Ib/sf 2,5 109.32 4.45E-04 lb/MMBtu 6 48.02 157.34 Methylene chloride(TH) dichloromethane) 3.16E-07 lb/sf 2,5 35.83 5.91E-07 lb/sf 2,5 24.72 60.55 Naphthalene (H) 8.13E-06 lb/MMBtu 6 2.38 8.13E-06 lb/MMBtu 6 0.88 3.26 Nickel metal(Co m onent of Nickel&Compounds)(TH) 1.17E-05 lb/MMBtu 6 3.43 1.17E-05 lb/MMBtu 6 1.26 4.69 Nitro henol,4-(H) 9.41E-08 lb/MMBtu 6 0.03 9.41E-08 lb/MMBtu 6 1 0.01 0.038 Pentachloro henol(TH) 4.48E-08 lb/MMBtu 6 0.01 4.48E-08 lb/MMBtu 6 0.00 0.018 Boise Cascade Wood Products-Moncure Plywood Emission Source(s): Fluidized Bed Wood Boiler and Two Direct Heated Dryers Source ID Number(s):ES-01,ES-09,ES-10,CD-02(multiclone on boiler) Emission Point(s): EP-09a-d,EP-10a-d 2016 Actual Process Throughput: 8,147 Boiler operating hours/yr 13,578 dry wood(ton/yr) 20,328 green wood(ton/yr) 400,819 MMBtu/yr Total Fuel Combusted 189,649 MMBtu/yr Green Wood Combusted 211,170 MMBtu/yr Dry Wood Combusted 113,581,000 sf/yr Hardwood Veneer Production 41,845,000 sf/yr Softwood Veneer Production 155,426,000 sf/yr Total Veneer Production 292,908 MMBtu/yr Btu of Wood Combusted-ratioed for Hardwood Veneer 107,912 MMBtu/yr Btu of Wood Combusted-ratioed for Softwood Veneer Actual Emissions Summary: Hardwood Softwood Total Compound Emission Factor Units Ref: Ib/ r Emissions* Emission Factor Units Ref. Emissions* Emissions* Ib/ r Ib/ r Perchloroeth lene PERC (tetrachloroeth lene)(TH) 2.46E-05 lb/MMBtu 6 7.21 2.46E-05 lb/MMBtu 6 2.65 9.86 Phenol TH 1.63E-06 lb/sf 2,5 185.42 3.41E-06 Ib/sf 2 142.69 328.11 Phosphorus Metal,Yellow or White H) 5.45E-03 lb/MMBtu 6 1596.35 5.45E-03 lb/MMBtu 6 588.12 2184.47 Polychlorinated bi hen is (TH) 7.41E-09 lb/MMBtu 6 0.002 7.41E-09 lb/MMBtu 6 0.0008 0.003 Pol c clic Organic Matter (H) 2.23E-05 lb/MMBtu 6 6.53 2.23E-05 lb/MMBtu 2 2.41 8.94 Pro ionaldeh de H) 9.08E-07 lb/sf 2,5 103.07 2.14E-05 lb/MMBtu 6 2.31 105.38 Propylene dichloride(H) 1,2 dichloro ro ane) 1.68E-05 lb/MMBtu 6 4.92 1.68E-05 lb/MMBtu 6 1.81 6.73 Selenium compounds(H) 5.39E-07 lb/MMBtu 6 0.16 5.39E-07 Ib/MMBtu 6 0.06 0.22 Styrene(TH) 3.87E-07 Ib/sf 2,5 43.96 1.54E-05 lb/MMBtu 6 1.66 45.62 Tetrachlorodibenzo- -dioxin,2,3,7,8- (TH) 1.10E-11 Ib/ODT 6 2.62E-07 1.10E-11 ib/ODT 6 2.62E-07 5.23E-07 Toluene(TH) 3.42E-07 Ib/sf 2,5 38.87 3.67E-06 lb/MMBtu 6 0.40 39.27 Trichlorobenzene, 1,2,4- H 6.75E-07 lb/sf 2,5 76.67 1.26E-06 lb/sf 2,5 52.78 129.44 Trichloroeth lene TH 1.99E-05 lb/MMBtu 6 5.83 1.99E-05 lb/MMBtu 6 2.15 7.98 Trichloroftuoromethane(CFC 111)(T) 1.59E-05 lb/MMBtu 6 4.66 1.59E-05 lb/MMBtu 6 1.72 6.37 Trichloro henol,2,4,6-(H) 2.76E-07 lb/MMBtu 6 0.08 2.76E-07 lb/MMBtu 6 0.03 0.111 Vinyl chloride(chloroethene)(TH) 2.32E-07 Ib/sf 2,5 26.38 4.34E-07 lb/sf 2,5 18.17 44.55 Vin lidene chloride(1,1-dichloroethene)(TH) 3.60E-07 Ib/sf 2,5 40.92 6.33E-07 lb/sf 2,5 26.50 67.42 X lene(TH) 3.95E-07 Ib/sf 2,5 44.81 1.87E-06 lb/sf 2 78.25 123.06 *Note: All emissions include emissions from wood combustion and wood drying. References: 1-Stack Testing Data, 1996 2-NCASI Wood Products Database,Updated 2013,Direct Fired Veneer Dryer 3-Based on Feb. 12,2010 stack test. PM10 assumed to be equal to PM. PM2.5 assumed to be 98% 4-OTM26:Interim VOC Measurement Protocol for the Wood Products Industry-July 2007 5-Half the average detection values are used for non-detects. 6-Tables 4.1,4.3,4.5,4.6,5.1 of NCASI TB 1013,March 2013,median values(metal factors with mechanical collector,for multiclone). Boise Cascade Wood Products -Moncure Plywood Emission Source(s): Fluidized Bed Wood Boiler and Two Direct Heated Dryers Source ID Number(s): ES-01,ES-09,ES-10, CD-02 (multiclone on boiler) Emission Point(s): EP-09a-d,EP-10a-d -Natural Gas burner for boiler start up 2016 Actual Process Throughput: Natural Gas 37 therms/yr 0.004 MMcf/yr I t Multiclone Natural Gas Control Emissions Compound Emission Factor(1) Eff.(2) (lb/yr) (TPY) CO 84lb/MMcf -- 0.000153 Ox 100lb/MMcf -- 0.000182 PM 7.6lb/MMcf 90% -- 0.000001 PM-10 7.61b/MMcf 90% -- 0.000001 PM-2.5 7.6lb/MMcf 90% -- 0.000001 SO2 0.61b/MMcf -- 0.000001 VOC 5.5lb/MMcf -- 0.000010 Arsenic 2.00E-04lb/MMcf 90% 7.30E-08 -- Benzene 2.10E-03 lb/MMcf 7.66E-06 -- Benzo(a)pyrene 1.20E-06 lb/MMcf 4.3 8E-09 -- Beryllium 1.20E-05lb/MMcf 90% 4.38E-09 -- Cadmium 1.10E-03 lb/MMcf 90% 4.01E-07 -- Chromium 1.40E-03lb/MMcf 90% 5.11E-07 -- Cobalt 8.40E-05lb/MMcf 90% 3.06E-08 -- _ _ Formaldehyde 7.50E-02 lb/MMcf 2.74E-04 -- Hexane 1.80E+00 lb/MMcf 6.57E-03 -- Lead 5.00E-04lb/MMcf 90% 1.82E-07 -- - Manganese 3.80E-04lb/MMcf 90% 1.39E-07 -- Mercury,vapor 2.60E-04 lb/MMcf 9.48E-07 -- Naphthalene 6.10E-04 lb/MMcf 2.23E-06 -- Nickel 2.10E-03lb/MMcf 90% 7.66E-07 -- POM 8.82E-05 lb/MMcf 3.22E-07 -- Selenium 2.40E-05lb/MMcf 1 90% 1 8.76E-09 -- ~ Toluene 3.40E-03 lb/MMcf 1 1.24E-05 -- Notes: 1. AP-42, Section 1.4,July 1998. Natural gas heating value of 1,020 Btu/cf and 100,000 Btu/therm. 2: Control efficiency from permit application applied to uncontrolled particulate emission factors. -S\Projects\ENV\60542933_BoiMon2017\500-Deliverables\CY 2016 AEI\Moncure 2016 AEI Calcs\FBB NG 6/13/2017 Boise Cascade Wood Products -Moncure Plywood Emission Source: Dry Waste System -Dry Waste Storage Silo Source ID Number: ES-12, CD-21 i Emission Point: EP-06,EP-12 2016 Actual Process Throughput: Plywood Production 88,938,000 sf/yr Emissions Summary: Compound Emission Factor Reference Emissions PM 9.29E-06 lb/sf 1 0.41 tpy PM 10 9.29E-06 lb/sf 1 0.41 tpy PM2.5 I 9.29E-06 lb/sf I 1 0.41 tpy References: 1. Emission factor from original Title V Permit Application i ' -ti I ' L Boise Cascade Wood Products -Moncure Plywood Emission Source: Sander System - Source ID Number: ES-04, CD-05 Emission Point: EP-05 r 2016 Actual Process Throughput: Sander Operation Production 20,320,000 sf/yr Emissions Summary: Compound Emission Factor Reference Emissions PM 1.15E-051b/sf 1 0.12 tpy PM10 1.15E-051b/sf 1 0.12 tpy PM2.5 1.15E-05lb/sf 1 0.12 tpy VOC 1.51E-04 lb/sf 2,3 1.54 tpy Acetaldehyde 1.77E-061b/sf 2 35.97 lb/yr Formaldehyde 1.22E-061b/sf 2 24.79 lb/yr Methanol 7.73E-06 lb/sf 2 157.07 lb/yr References: 1. Stack Testing Data, 1995 2. Emission factors for VOC and organics based on NCASI Database for Wood Products •_- Manufactures,Updated February 2013, Sander,softwood plywood,uncontrolled median factor 3. VOC calculated as sum of VOC as C,formaldehyde,and 50%of methanol factors. � I Boise Cascade Wood Products -Moncure Plywood Emission Source: Dry Waste Transfer System Source ID Number:ES-03 CD-06 Emission Point: EP-06 2016 Actual Process Throughput: Hardwood Plywood Production 46,653,000 sf/yr Softwood Plywood Production 42,285,000 sf/yr Emissions Summary: Softwood Hardwood - Compound Emission Factor Ref. Emission Factor Ref. Emissions PM 6.60E-04 lb/sf 1 1.15E-05 lb/sf 1 14.22 tpy PM10 6.60E-04 lb/sf 1 1.15E-05 lb/sf 1 14.22 tpy PM2.5 6.60E-04 lb/sf 1 1.15E-05 lb/sf 1 14.22 tpy References: 1. Emission factor from original Title V Permit Application II Boise Cascade Wood Products -Moncure Plywood Emission Source: Hog Fuel Storage Silo Source ID Number: IES-GWS (ES-11) Emission Point: EP-11 2016 Actual Process Throughput: ' I Hog Fuel 19,128 ton/yr - - Emissions Summary: Emissions are calculated use the"drop loading equation"from AP-42 Section 13.2.4(Aggregate Handling and Storage Piles),November 2006. AP-42 Section 13.2.4: '3 (U i E (lb/ton) =k x 0.0032 x ` 5 ( ) M 11.a where: 2 J E= emission factor k= particle size multiplier(dimensionless) U= mean wind speed(mph) M= material moisture content(%) k= 0.74 For PM k= 0.35 For PMia k= 0.053 For PM2.5 U= 6.88 mph for Charlotte,NC(nearest major city)from 2008-2012 Charlotte met data M= 50 %,Wood assumed to have average moisture content of 50%based on AP-42, Section 1.6,Wood Residue Combustion in Boilers, Sept.2003 Therefore,emission factors(lb PM per ton)_ PM factor= 3.96E-05 lb/ton —� PMio factor= 1.87E-05 lb/ton PM2_5 factor= 2.83E-06 lb/ton Compound Emission Factor Emissions PM 3.96E-05 lb/ton 0.00038 tpy PM10 1.87E-05 lb/ton 0.00018 tpy PM2.5 2.83E-06 lb/ton 0.00003 tpy �t { Boise Cascade Wood Products -Moncure Plywood Emission Source: Green Chip Sizing,Rechip, Transfer -- Source ID Number: ES-17,ES-18,ES-14 Emission Point: EP-14 2016 Actual Process Throughput: Tons Green Chips 23,134 ton/yr i Emissions Summary: Emissions are fugitive in nature. Specific emission factors are not available for rechipping operations. Rechipping emissions are Cassumed to be similar to emissions from debarking. PM emissions for debarking are based on the former AP-42 emission factor for drum debarkers and total amount of green material processed by the rechipper;PM2.5= 19%of PM. PM 0.024 lb/ton PM 10 0.011 lb/ton PM2.5 0.0046 lb/ton Green Emission Annual Annual Compound Material Factor Emissions Emissions (tpy) (lb/ton) (lb/yr) (TPY) PM 23,134 0.024 555.22 0.28 I! PM 10 23,134 1 0.011 254.47 0.13 PM2.5 23,134 0.0046 105.49 0.05 I iW "r Boise Cascade Wood Products -Moncure Plywood Emission Source: Plywood Waste Hog Source ID Number: ES-16 Emission Point: EP-16 2016 Actual Process Throughput: Tons Dry Wood 13,578 ton/yr Emissions Summary: Emissions are fugitive in nature. Specific emission factors are not available for rechipping operations. Rechipping emissions are b assumed to be similar to emissions from debarking. PM emissions for debarking are based on the former AP-42 emission factor for drum debarkers and total amount of green material processed by the rechipper;PM2.5= 19%of PM. I PM 0.024 lb/ton PM 10 0.011 lb/ton PM2.5 0.0046 lb/ton pp Green Emission Annual Annual Compound Material Factor Emissions Emissions (tpy) (lb/ton) (lb/yr) (TPY) PM 13,578 0.024 325.88 0.16 PM10 13,578 0.011 149.36 0.07 PM2.5 13,578 0.0046 61.92 0.03 a i r k Boise Cascade Wood Products -Moncure Plywood Emission Source(s): Glue Operations and Pressing Source ID Number(s): ES-13 Emission Point: EP-13 �1 2016 Actual Process Throughput: i - Hardwood Plywood Production 46,653,000 sf/yr q Softwood Plywood Production 42,285,000 sf/yr Hardwood Softwood Total u Compound Emission Units Ref. Emissions Emission Emissions Emissions Factor Units Ref. ton/ r Factor . ton/ r ton/ r PM 2.00E-04 lb/sf 1 4.67 2.00E-04 lb/sf 1 4.23 8.89 PM10 2.00E-04 lb/sf 1 4.67 2.00E-04 Ib/sf 1 4.23 8.89 PM2.5 1 8.32E-05 lb/sf 1 1.94 8.32E-05 Ib/sf 1 1.76 3.70 VOC(WPPI) I 1.71E-04 lb/sf 1 2 1 3.99 1 5.87E-04 lb/sf 1­27 12.41 16.40 4 Hardwood Softwood Total Compound Emission Units Ref. Units Ref. Emissions Emission Emissions Emissions Factor . lb/ r Factor . Ib/ r lb/ r Acetaldehyde -- 1 3.61E-06 Ib/sf 1 152.65 152.65 Formaldehyde 5.00E-06 lb/sf 2 233.27 5.00E-06 lb/sf 2 211.43 444.69 Methanol 1.11E-04 lb/sf 2 5178.48 1.11E-04 lb/sf 2 4,693.64 9,872.12 e: Methyl Ethyl Ketone -- 1 ; 8.12E-07 lb/sf 1 34.34 34.34 Methyl Isobutyl Ketone -- 1 8.17E-07 lb/sf 1 34.55 34.55 Phenol 1.59E-05 lb/sf 1 741.78 2.71E-06 lb/sf 1 1 114.59 856.38 C1 References: 1 1. NCASI Wood Products Database,Updated February 2013,median value, "--" signifies non-detect. Mill uses PF resin, so PF factors are used when available.Hardwood HAPs are not available for PF resin,so OF resin is used as best available data. PM10 is assumed to equal PM,and PM2.5 is assumed to equal condensable PM. Softwood factors for PM are used,as hardwood factors are not available. 2. Press Compliance Test on December 10,2014. The WPP I VOC factor was developed per EPA OTM-26 method. i J I �I F I` Boise Cascade Wood Products-Moncure Plywood Emission Source: 250 HP Diesel-Fired Water Pump #1 - Source ID Number: ES-19 2016 Actual Process Throughput: Hours of Operation 83 Hr/yr No.2 Fuel Oil Usage 952 gal/yr i Heat Input(250 hp) 52.8 MMBtu/yr Compound Emission Factor Units Reference Emissions ton/ r CO 9.50E-01 lb/MMBtu 1 0.025 Ox 4.41E+00 lb/MMBtu 1 0.116 PM 3.10E-01 lb/MMBtu 1 0.008 PM10 3.10E-01 lb/MMBtu 1 0.008 PM2.5 3.10E-01 lb/MMBtu 1 0.008 S02 2.90E-01 lb/MMBtu 1 0.008 VOC 3.50E-01 lb/MMBtu 1 0.009 .� Compound Emission Factor Units Reference Emissions lb/ r Acetaldehyde(TH) 7.67E-04 lb/MMBtu 1 0.040 Acrolein(TH) 9.25E-05 lb/MMBtu 1 0.005 Benzene(TH) 9.33E-04 lb/MMBtu 1 0.049 Benzo(a)pyrene (T) 1.88E-07 lb/MMBtu 1 0.00001 ='h Formaldehyde(TH) 1.18E-03 lb/MMBtu 1 0.062 I Naphthalene (H) 8.48E-05 lb/MMBtu 1 0.004 Toluene(TH) 4.09E-04 lb/MMBtu 1 0.022 Xylene(TH) 2.85E-04 lb/MMBtu 1 0.015 POM 1.68E-04 lb/MMBtu 1 0.009 References: 1 -AP-42, Section 3.3,Table 3.3-1,October 1996 1 _r `n n j Boise Cascade Wood Products -Moncure Plywood Emission Source: 250 HP Diesel-Fired Water Pump #2 Source ID Number: ES-23 2016 Actual Process Throughput: Hours of Operation 16 Hr/yr No.2 Fuel Oil Usage 416 gal/yr Heat Input(250 hp) 10.2 MMBtu/yr I! Compound Emission Factor Units Reference Emissions ton/ r CO 9.50E-01 lb/MMBtu 1 0.005 Ox 4.41E+00 lb/MMBtu 1 0.022 �1 PM 3.10E-01 lb/MMBtu 1 0.002 PM10 3.10E-01 lb/MMBtu 1 0.002 PM2.5 3.10E-01 lb/MMBtu 1 0.002 SO2 2.90E-01 lb/MMBtu 1 0.001 VOC 3.50E-01 lb/MMBtu 1 0.002 Compound Emission Factor Units Reference Emissions _ Ib/ r Acetaldehyde(TH) 7.67E-04 lb/MMBtu 1 0.008 Acrolein(TH) 9.25E-05 lb/MMBtu 1 0.001 Benzene(TH) 9.33E-04 lb/MMBtu 1 0.009 Benzo(a)pyrene (T) 1.88E-07 lb/MMBtu 1 0.000002 r A Formaldehyde(TH) 1.18E-03 lb/MMBtu 1 0.012 iNaphthalene (H) 8.48E-05 lb/MMBtu 1 0.001 Toluene(TH) 4.09E-04 lb/MMBtu 1 0.004 Xylene(TH) 2.85E-04 lb/MMBtu 1 0.003 POM 1.68E-04 lb/MMBtu 1 0.002 References: �i 1 -AP-42, Section 3.3,Table 3.3-1, October 1996 i k G a I Boise Cascade Wood Products -Moncure Plywood � f Emission Source(s): Vat Operations Source ID Number(s): ES-20 Emission Point: EP-20 2016 Actual Process Throughput: Total Vat Production 82,800,000 sf/yr Compound Emission Factor Units Reference Emissions ton/ r VOC-Hardwood 1.20E-05 lb/sf 1,2 0.26 VOC-Softwood 7.70E-05 lb/sf 1,2 1.55 Total VOC 1.81 Compound Emission Factor Units Reference Emissions lb/ r Acetaldehyde 4.67E-06 lb/sf 1 386.68 Methanol 7.34E-06 lb/sf 1 607.75 References: 1. NCASI Database for Wood Products Manufacturers,update February 2013,median, Softwood plywood log vat. VOC hardwood is sum of VOC compounds excluding pinenes; --•� VOC softwood is sum of VOC compounds plus pinenes. (These values are same as AP-42 10.5,but with more significant figures.) -j 2. Hardwood and softwood vat production is ratioed based on log throughput(gum and poplar vs pine,respectively). i u .J' Ire N Boise Cascade Wood Products -Moncure Plywood Emission Source(s): End Sealer Spray Booth Source ID Number(s): ES-21 Emission Point: EP-21 2016 Actual Process Throughput: End Seal Material Usage 540 gal/yr Estimated Overspray 30.0% 3 Spray Booth Filter Efficiency 97.5% *` Compound Emission Factor Units Ref Emissions ton/ r PM 90% %wt 1 0.01 PM10 90% %wt 1 0.01 VOC 0.4% %wt 2 0.01 - Compound Emission Factor Units Ref Emihs/it ns Vinyl acetate 0.031% %wt 2,3 1.34 References: 1. Conservatively assume 90%solids in material.Assume 30%overspray into filter. 2. Compound speciation from SDS,April 2010. Specific gravity is 0.96. 3. Compound speciation from WVCO letter,April 26,2012. I a �i a h t, �I r Boise Cascade Wood Products -Moncure Plywood Emission Source: Tongue and Groove Saw Source ID Number: ES-22, CD-06 Emission Point: EP-06 r- j_, 2016 Actual Process Throughput: Saw Operating Hours 54 hours �- Saw Production 354,000 sf/yr j� Calculations for this source are based on the following assumptions: 4 The T&G saw removes 0.5"per panel. The T&G saw trims the finished plywood panels of 96"x 48". The nominal thickness is 3/8" (0.375). The density of dry pine is 35.6 lb/ft3. �. Conservatively assume baghouse efficiency of 99.5%. 'x Volume of Annual T&G- T&G Compound Total Panels T&G/Panel Dust Generated Rate (per year) (ft3/panel) (ton/yr) (ton/hr) PM 11,063 0.0104 2.051 0.038 Emissions Summary Baghouse Annual Compound Efficiency Emissions (%) (lb/yr) (ton/yr) PM 99.5 20.51 0.010 PM10 z 99.5 1 6.58 0.003 PM2.5 z 99.5 2.93 0.001 Compound Emission Factor Reference Emissions VOC 7.55E-05 lb/sf 3 0.01 tpy Acetaldehyde 5.59E-07 lb/sf 3 0.20 lb/yr Formaldehyde 3.89E-07 lb/sf 3 0.14 lb/yr 6 Methanol 6.82E-06Ib/sf 3 2.41 lb/yr References: 1. Emission rates for PM based on estimated amount of trim and dust generated and conservative baghouse efficiency of 99.5%. 2. AP-42 Appendix 13.1, Section 10.5,October 1986. PM10 is assumed to be 32.1%of PM from V sander cyclone and baghouse. PM2.5 is assumed to be 14.3%of PM from sander cyclone and baghouse. 3. Emission factors for VOC and organics based on NCASI Database for Wood Products Manufactures, _ updated February 2013, Saw,softwood plywood,uncontrolled median factor. VOC calculated as sum of VOC as C,formaldehyde,and 50%of methanol factors. I s j Boise Cascade Wood Products -Moncure Plywood i, Emission Source: Bark Hog P } Source ID Number: IS-IN-1 Emission Point: IS-IN-1 2016 Actual Process Throughput: 1 � Fuel Hogged 19,128 ton/yr I� i Emissions Summary: ti.. Emissions are fugitive in nature. i Specific emission factors are not available for hogging operations. Hogging emissions are assumed to be similar to emissions from debarking. PM emissions for debarking are based on the former AP-42 emission factor for drum debarkers and total amount of green material processed by the hogs;PM2.5= 19%of PM. The hog is located inside a building. A 95%control has been applied to account for building control. r PM 0.024 lb/ton " p PM 10 0.011 lb/ton PM2.5 0.0046 lb/ton Green Emission Inside Annual Annual ' la Compound Material Factor Building Emissions Emissions (tpy) (lb/ton) Control(%) (lb/yr) (TPY) PM 19,128 0.024 95% 22.95 0.01 PM10 19,128 0.011 95% 10.52 0.01 PM2.5 19,128 0.0046 95% 4.36 0.002 ' i i u I 1 V ti r-- N Boise Cascade Wood Products -Moncure Plywood Emission Source: Core Chipping Source ID Number: IS-IN-2 Emission Point: IS-IN-2 J 2016 Actual Process Throughput: Cores Chipped 58 ton/year Emissions Summary: Emissions are fugitive in nature. Specific emission factors are not available for chipping operations. Chipping emissions are assumed to be similar to emissions from debarking. PM emissions for debarking are based on the former AP-42 emission factor for drum debarkers and total amount of green material processed by the chipper;PM2.5= 19%of PM. The chipper is located inside a building. A 95%control has been applied to account for building control. PM 0.024 lb/ton PM10 0.011 lb/ton PM2.5 0.0046 lb/ton Green Emission Inside Annual Annual Compound Material Factor Building Emissions Emissions (tpy) (lb/ton) Control(%) (lb/yr) (TPY) PM 58 0.024 95% 0.07 3.48E-05 PM10 1 58 1 0.011 95% 0.03 1.60E-05 PM2.5 1 58 1 0.0046 95% 0.01 6.61E-06 i u r-- i !' Boise Cascade Wood Products -Moncure Plywood Emission Source: Green Veneer Hogging Operations Source ID Number: IS IN-3 Emission Point: IS—IN-3 2016 Actual Process Throughput: Green Veneer Hogged 23,076 ton/year �l r Emissions Summary: Emissions are fugitive in nature. Specific emission factors are not available for hogging operations. Hogging emissions are assumed to be similar to emissions from debarking. PM emissions for debarking are based on the former AP-42 emission factor for drum debarkers and total amount of green material processed by the hogs;PM2.5= 19%of PM. The hog is located inside a building. A 95%control has been applied to account for building control. t_z PM 0.024 lb/ton PM10 0.011 lb/ton PM2.5 0.0046 lb/ton Green Emission Inside Annual Annual Compound Material Factor Building Emissions Emissions (tpy) (lb/ton) Control(%) (lb/yr) (TPY) PM 23,076 0.024 95% 27.69 0.01 PM10 23,076 1 0.011 95% 12.69 0.01 PM2.5 23,076 0.0046 95% 5.26 0.003 � " ,_J Boise Cascade Wood Products -Moncure Plywood Emission Source: Ink and Painting Operations Source ID Number: IS-IN-4,IS-IN-5 Emission Point: IS-IN-4,IS-IN-5 2016 Actual Process Throughput: Logo paint usage 0 gal/yr { Ink usage 175 gal/yr Ink density 8.21 lb/gal Emissions Summary: Compound Emission Factor Reference Emissions �- VOC-logo paint 4.00E-01 lb VOC/gal 1 0.00 tpy VOC-ink 2.00E-01 lb VOC/lb 1 0.14 tpy fIlTotal VOC 0.14 tpy References: 1. Safety Data Sheets ` i I f IF^- I Boise Cascade Wood Products -Moncure Plywood Emission Source: Plywood Surface Patching Source ID Number: IS-IN-6 Emission Point: IS-IN-6 2016 Actual Process Throughput: Plywood Surface Patching(Part A) 2,970 gal/yr l Density 12.58 lb/gal Plywood Surface Patching(Part B)l 330 gal/yr Density 10.33 lb/gal V Plywood Surface Patching(W.B.Face) 660 gal/yr + Emissions Summary: Emissions Compound Component Units Reference lb/ r tons/ r VOC-U-100-A Patch 0.02% %wt 2 7.5 0.00 VOC-W.B.Face 0.25 lb/gal 3 165.0 0.08 MDI-U-100-B Patch 38% %wt 1 negligible negligible References: 1. Safety Data Sheet for U-100-B Patch Catalyst,April 2014. Due to the extremely low vapor pressure of the material(<0.000001 mmHg)per the manufacturer's SDS,VOC and HAP emissions from the use of this product are assumed to be negligible. (The SDS shows 0%VOC.) 2. Safety Data Sheet for U-100-A Patch,April 2014. 3. Safety Data Sheet for Putty W.B.Face-Pine,January 1994. SDS states there are no reportable quantities of ingredients present and no chemicals subject to reporting requirements. I ' b 1 ~r Boise Cascade Wood Products -Moncure Plywood Emission Source: Maintenance Parts Washer Source ID Number: IS-IN-7 L ;e Emission Point: IS-IN-7 2016 Actual Process Throughput: Gallons Purchased: 0 gal/yr i Emissions Summary: Compound Emission Factor Reference Emissions VOC 6.58 lb/gal 1 0.00 tpy i -- References: 1. Safety Data Sheet r; 4 nh Boise Cascade Wood Products -Moncure Plywood Emission Source: Veneer Diverter Exhaust Cyclone Source ID Number: IS4N-8 Emission Point: IS-IN-8 2016 Actual Process Throughput: Green Veneer 155,347 ton/yr Emissions Summary: Compound Emission Factor Reference Emissions PM 1.40E-02 lb/DT 1 0.54 tpy PM 10 1.40E-02 I lb/DT 1 0.54 tpy References: 1. Weyerhaeuser Test Data,Title V Bulletin#19,average green chips factor i i a. i, Boise Cascade Wood Products -Moncure Plywood Emission Source: Green Veneer Stackers Source ID Number: IS-IN-9, IS-IN-10 Emission Point: IS-IN-9, IS-IN-10 2016 Actual Process Throughput: r--, Green Veneer 155,347 ton/yr Emissions Summary: i Compound Emission Factor Reference Stacker Emissions PM 1.40E-02 lb/DT 1 0.54 tpy PM10 1.40E-02 lb/DT 1 0.54 tpy References: 1. Weyerhaeuser Test Data,Title V Bulletin#19,average green chips factor R i t Boise Cascade Wood Products-Moncure Plywood Emission Source: Hammer Hog Truck Dump Source ID Number: IS-IN-11 Emission Point: IS-IN-11 2016 Actual Process Throughput: Dry waste 1,517 ton/yr Emissions Summary: Emissions are calculated use the"drop loading equation"from AP-42 Section 13.2.4(Aggregate Handling and Storage Piles),November 2006. r U 113 AP-42 Section 13.2.4: 15 J 1 E(lb/ton) =k x 0.0032 x (` 14 where: ` 2 E= emission factor k= particle size multiplier(dimensionless) U= mean wind speed(mph) M= material moisture content(%) k= 0.74 For PM k= 0.35 For PMIO k= 0.053 For PM2.5 -, U= 6.88 mph for Charlotte,NC(nearest major city)from 2008-2012 Charlotte met data M= 50 %,Wood assumed to have average moisture content of 50%based on AP-42, Section 1.6, Wood Residue Combustion in Boilers, Sept.2003 Therefore,emission factors(lb PM per ton)= PM factor= 3.96E-05 lb/ton PMIO factor= 1.87E-05 lb/ton PM25 factor= 2.83E-06 lb/ton Compound Emission Factor Emissions PM 3.96E-05Ib/ton 3.00E-05 tpy - P1410 1.87E-05 lb/ton 1.42E-05 tpy 1 - PM2,:5 2.83E-06 lb/ton 2.15E-06 tpy 1 i r � Boise Cascade Wood Products -Moncure Plywood Emission Source: Dry Waste Truck Dump Source ID Number: IS-IN-12 Emission Point: IS-IN-12 i 2016 Actual Process Throughput: Dry waste 1,243 ton/yr Emissions Summary: Emissions are calculated use the"drop loading equation" from AP-42 Section 13.2.4(Aggregate Handling and Storage Piles),November 2006. rU113 AP-42 Section 13.2,4: 15 J E (Ib/ton) =k x 0.0032 x (m)1.4 where: E= emission factor k= particle size multiplier(dimensionless) U= mean wind speed(mph) ,i M= material moisture content(%) k= 0.74 For PM k= 0.35 For PM10 k= 0.053 For PM2.s U= 6.88 mph for Charlotte,NC(nearest major city)from 2008-2012 Charlotte met data M= 50 %,Wood assumed to have average moisture content of 50%based on AP-42, Section 1.6,Wood Residue Combustion in Boilers, Sept.2003 Therefore,emission factors(lb PM per ton)_ PM-factor= 3.96E-05 lb/ton -- PM10 factor= 1.87E-05 lb/ton _ PM2.5 factor= 2.83E-06 lb/ton Compound Emission Factor Emissions PM 3.96E-05 lb/ton 2.46E-05 tpy AM10 1.87E-05 lb/ton 1.16E-05 tpy P.M2.5 '` 2.83E-06 lb/ton 1.:76Er06 tpy r `y i � I Boise Cascade Wood Products -Moncure Plywood Annual Activity and Usage Information 2016 Air Emissions Inventory ; i _ Activity and Usage 2016 Annual Amount Green Veneer Hogging Operations 23,076 ton/yr t Maintenance Parts Washer Sol'n Purchased 0 gal/yr End Seal Paint 540 gal/yr Paint Usage(Logo painting) 0 gal/yr Miscellaneous Ink Usage 175 gal/yr Green Veneer Stackers 155,347 ton/yr Plywood Surface Patching(W.B.Face) 660 gaUyr Plywood Surface Patching(Part A) 2,970 gal/yr ' Plywood Surface Patching(Part B) 330 gal/yr Cores Sold in 2016 657,208 cores Ash Total Wood Ash 213 tons Total Wood Ash sent offsite 213 tons PF Resin Usage PF Resin Application Rate 29 Tons/MMSF PF Resin Usage 3,019 tons 1. Bark fired is calculated based on log usage and percentage of a log that is bark(assumes 80%of bark originally on log is combusted). Dry fuel is estimated to be 15%of total fuel usage based on data from Chester Plywood(sister plant). 2. Heat Content is Chester Plywood fuel analysis data. i r ` Q:\DCS\Projects\ENV\60542933_BoiMon2017\500-Deliverables\CY 2016 AEI\Moncure 2016 AEI CalesTrod Info -Z i Appendix E Supporting Data IL I �� '17/17, 8:52 AM NC DAQ-EMISSIONS INVENTORY Division • � ��1 Home Emissions Flow Facility Totals ES-CD List User Manual Logoff Operating Scenario Summary AERO Emission Sources Emission Groups Control Devices Emission Release Points Operating Scenario Summary Closeout PAGE INSTRUCTIONS Facility Id : 1900039 Data Year:2016 < Back Continue> Find Operating Scenario OS Not Id Description Status Operated GR2 Green Veneer Stackers Q OS32 Green Veneer Stackers O Add New Operating Scenario G-24 Veneer dryers and heat source(wood burner) Q OS26 Veneer dryers and heat source(wood burner) Ibs/SF, (Softwood) O OS27 Veneer dryers and heat source(wood burner) HAPS Ib/mmBtu, (Softwood) OS30 Veneer dryers and heat source(wood burner) Ibs/SF, (Hardwood) OS31 Veneer dryers and heat source(wood burner) HAPS Ib/mmBtu, O (Hardwood) OS36 Natural Gas start up burner(1 MMBtu/hr) Add New Operating Scenario G-25 Ink and painting operations Q OS5 Ink and painting operations Add New Operating Scenario G-27 Woodwaste Transfer system Q OS20 Woodwaste Transfer(Rechipper)system Add New Operating Scenario ES-13-25HP 25 panel hot press Q Add New Operating Scenario ES-13-40HP 40 panel hot press Add New Operating Scenario ES-13-CC Curtain coater Q Add New Operating Scenario ES-1 3-PO Paper overlay operation Q Add New Operating Scenario ES-1 3-PS Plywood spreader Q Add New Operating Scenario ES03-CC Core composer with saw Add New Operating Scenario ES03-CS Core saw(green or dry veneer) Add New Operating Scenario ES03-PSS Panel sawing system https:Hxapps.ncdenr.org/aq/EDExternalServlet?url=TO—OSSummary_Page I of 3 5/17/17,8:52 AM NC DAQ-EMISSIONS INVENTORY Add New Operating Scenario ES03-SMS-1 String machine including saws OS21 Dry Waste transfer system Add New Operating Scenario ES03-SMS-2 String machine including saws Add New Operating Scenario ES03-SS Strip saw Q Add New Operating Scenario ES04 Wood sander Q OS12 wood sander Add New Operating Scenario ES12 Dry wood residual storage silo Q OS17 dry wood residual storage silo Add New Operating Scenario ES13-GMO Glue mixing operations consisting of two resin storage tanks and four mixe OS10 glue mixing,application and hot presses operations(Hardwood) OS28 glue mixing,application and hot presses operations, (softwood) Add New Operating Scenario ES16 Plywood waste hog Q OS9 plywood hog Add New Operating Scenario ES20 Vat operations OS18 Vat Operations: Heating of Blocks Add New Operating Scenario ES21 Edge sealer spray booth OS33 End Sealer Spray Booth Add New Operating Scenario ES22 Tongue and groove saw(plywood finishing) Q OS34 Tongue and Groove Saw O Add New Operating Scenario 1-1 Bark hogging operations with two saws Q OS2 Bark hogging operations O Add New Operating Scenario 1-11 hammer hog truck dump Q OS25 Hammer hog truck dump- no controls O Add New Operating Scenario 1-12 dry waste truck dump Q OS24 Dry Waste truck dump O Add New Operating Scenario 1-2 Core chipping and handling Q OS3 Core chipping and handling operations O Add New Operating Scenario 1-3 Green veneer hogging Q OS4 Green veneer hogging operations O https:Hxapps.ncdenr.org/aq/EDExternalServiet?url=TO—OSSummary_Page 2 of 3 '17/17,8:52 AM NC DAQ-EMISSIONS INVENTORY Add New Operating Scenario 1-6 Plywood surface patching Q OS6 Plywood surface patching Add New Operating Scenario 1-7 Maintenance parts washers a OS7 Maintenance parts washer Add New Operating Scenario 1-8 Veneer diverter exhaust cyclone 13 OS8 Veneer diverter exhaust cyclone Add New Operating Scenario IES-19 Diesel-fired water pump(250 Horsepower maximum power output)for emergenc OS11 250 horsepower diesel-fired water pump o OS35 250 HP Diesel Fired Water Pump#2-IES23 Add New Operating Scenario IES-23 Diesel-fired fire pump emergency engine(250 Horsepower maximum power outpu OS37 250 HP Diesel-Fired Water Pump#2 Add New Operating Scenario IES-GWS Green wood fuel storage silo Q OS16 Green wood fuel storage silo O Add New Operating Scenario < Back Continue> Feedback Top of Page https:Hxapps.ncdenr.org/aq/EDExternalServlet?url=TO—OSSummary_Page 3 of 3 Boise Cascade Wood Products -Moncure Plywood Annual Activity and Usage Information 2016 Air Emissions Inventory Activity and Usage 2016 Annual Amount Vat Production 82,800,000 ft (3/8") Hardwood Veneer Production 113,581,000 ftZ(3/8") Softwood Veneer Production 41,845,000 ftZ(3/8") Hardwood Plywood Production 46,653,000 ftZ(3/8") ' Plywood Production Softwood Plywood Production 42,285,000 ftZ(3/8") Plywood Press Hours of Operation 5,458 hours _ Sander Production 20,320,000 ftZ(3/8") T&G Saw Production 354,000 ftZ(3/8") T&G Saw Hours of Operation 54 hours Pine Logs 94,426 tons Log Throughput Gum Logs 83,038 tons Poplar Logs 16,720 tons Boiler Hours of Operation 8,147 hours Total Dry Wood Combusted' 13,578 ton(as fired) Dry Wood Heat Content 7,776 Btu/lb Total Dry Wood Combusted 211,170 MMBtu/yr - Green Chips Purchased for Combustion 0 tons chips Green Chips Combusted 1,200 tons chips Green Chips Heat Content 4,541 Btu/Ib Total Green Chips Combusted 10,898 MMBtu Total Hog Fuel-Combusted' 19,128 ton(as fired) Plant wide Fuel Poplar Bark Heat ContentZ 5,703 Btu/lb Combustion Gum Bark Heat ContentZ 4,952 Btu/lb Pine Bark Heat ContentZ 4,018 Btu/lb Total Hog Fuel Combusted 178,751 MMBtu Total Green Fuel Combusted 189,649 MMBtu Total of All Fuel Combusted 400,819 MMBtu Boiler Efficiency 86.0 % Natural Gas Combusted 37.21 therms 250 HP Diesel Fired Water Pump#1 952 gal/yr 83 hr/yr 250 HP Diesel Fired Water Pump#2 416 gal/yr 16 hr/yr Veneer Diverter 155,347 ton/yr Miscellaneous Hammer Hog Truck Dump 1,517 ton/yr Dry Waste Truck Dump 1,243 ton/yr Core Chipping and Handling 58 ton/yr Q:\DCS\Projects\ENV\60542933_BoiMon2019\500-Deliverables\CY 2016 AEMoncure 2016 AEI Calcs\Prod Info