AQ_F_1900039_20150630_EI_Cmb-EI-File

2014 Emissions Inventory Review / Data Tracking Form
Facility Name: Moncure Plywood Facility ID: 1900039
Facility Assigned to: Data Entry: Chatham County
Classification: Maureen Conner I Confidential Copy Submitted?
Title V ❑l 1 YES
NO
Initial Review/Data Entry
❑ Enter date received into ED. Date Received:
❑ Assigned to appropriate individual. Date Assigned: Date Due:
p Paper copy submitted: One copy received with supporting documentation,certification form signed by responsible official,and
yappears generally complete;OR
p/Electronic copy submitted: All supporting documentation and certification form(with time/date stamp)signed by responsible
official has been received.
Comments:
Inventory Review
Er All forms and supporting documentation appear to be complete if paper submission(check ED OS data if electronic).
C" Contact,address,phone number changes entered into I-Beam/Facilities if necessary.
@KAll 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.
Cl"'Check if SCC codes for each OS are accurate and update if needed.
GJ"'Evaluate"U"sources for significance and address according to policy.
Calculations/forms appear to add up correctly.
ET" All compliance issues are being addressed(e.g.Toxics limits,above TV thresholds,large emissions increase/decrease,installation
�thout a permit).
1 volatile HAPs/TAPS were included in the VOC total.
ER Calculations and control efficiencies appear correct. Emission factors are the best available and most current factors appropriate
or the reporting facility(e.g. stack testing,AP-42,etc.).
Review facility comments and address any issues.
Ii"Update ED(Data Entry Main)if additional information is required(corrections due date and date received).
[EK heck all ED QA/QC reports.
[�/Comparison with previous emission inventory must be made and outliers(> 10%)must be investigated and explained.
L V 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:
1!,�.=
Date Review Complete: `O- 114- U1 Signature: �-w--
Date Submitted to EI Coordinator: lU-
Date Approved: 1 Initials: Vv

Facility Total CY 2014 Emission Summary Recorded in ED Facility ED#: 1900039
Facility Name: Moncure Plywood Permit#(s): 03424T24
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 emissiol No GHGs
times their 1995 IPCC Global Warming Potential(GWP), Reported
converted to metric tons)
Criteria Pollutants Actual Emissions
(Tons/Year)
Pollutant CAS CY 2014 CY-2013 Demini- %
from ED from Fees mus Change
CO CO 30.06 29.28, 0.5 2.7%
NOx NOx 48.06 44.14 0.5 .8.9%
PM(TSP) TSP 59.89 66.42 .0.5 -9.8%
PM10 PM10 59.85 66.40 0.5 -9.9%
PM2.5 PM2.5 49.52 55.20 0.5 1 -10.3%
S02 S02 0.760000 0.700000 0.5 8.6%
VOC VOC 71.40 63.30 - 0.5 12.8%
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants(TAPs)
(Pounds/Year)
Pollutant CAS CY 2014 CY 2013 Demini- %
from ED from Fees mus Change
Arsenic& Compounds(total mass of elemental AS, arsine and 1.52 1.39 0.01 19.4%
all inorganic compounds)
Arsenic Unlisted Compounds- Specify Compound ASC-Other 1.52 1.39 0.01 8.7%
(Component of ASC)
Cadmium & compounds(total mass includes elemental metal) 2.24 2.06 0.1 8.7%
Cadmium Metal, elemental, unreacted(Component 4 7440-43-9 2.24 2.06 0.1 8.7%
CDC)
Cadmium Unlisted Compounds- Specify Compounc CDC-Other 0.000160 Not 0.1 N/A
(Component of CDC) Reported
Chromium-All/TotaI(includes Chromium(VI) categories, 14.58 13.41 0.1 18.7%
metal and others)
Chromic acid (VI) (Component of So1CR6 & CRC) 7738-94-5 3.28 3.02 0.01 F8.70%/.
10/15/2015 Page 1 of 4

Facility Total CY 2014 Emission Summary Recorded in ED Facility ID #: 1900039
Facility Name: Moncure Plywood Permit#(s): 03424T24
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPs) (Pounds/Year)
Pollutant CAS CY 2014 CY 2013 Demini- %
from ED from Fees mus Change
Chromium Unlisted Compounds- Specify Compoun CRC-Other 11.30 10.39 0.1 8.7%
(Component of CRC)
Chromium (VI)Soluble Chromate Compounds(Component of 3.28 3.02 0.01 18.6%
CRC)
Chromic acid (VI) (Component of SolCR6 &CRC) 7738-94-5 3.28 3.02 0.01 8.7%
Lead& compounds Z25 6.67 1.0 8.7%
Lead Unlisted Compounds- Specify Compound PBC-Other 7.25 6.67 10.0 8.7%
(Component of PBC)
Manganese&compounds 1,172.06 1,078.45 10.0 18.7%
Manganese Unlisted Compounds- Specify Compow NiNG=Other 1,172.06 1,078.45 10.0 8.7%
(Component of MNC)
Mercury & Compounds-all total mass includes Hg Vapor 0.541710 0.498080 0.001 8.8%
Mercury, vapor(Component of HGC) 7439-97-6 0.541710 0.498080 0.001 8.8%
Nickel& Compounds,sum total mass includes elemental 5.51 5.07 1.0 8.7%
Nickel metal (Component of NIC) 7440-02-0 5.51 5.07 1.0 8.7%
Nickel Unlisted Compounds(Component of NIC - NIC-Other 0.000310 Not 1.0 N/A
Specify) I Reported
Polycyclic Organic Matter(Specific Compounds from OAQPS 3.84 3.53 1.0 8.8%
for M
Naphthalene (Component of 83329/POMTV) 91-20-3 3.84 3.53 1.0 8.7%
Acetaldehyde 75-07-0 29194.42 2,352.32 10.0 -6.7%
Acrolein 107-02-8 382.95 342.28 10.0 11.9%
Benzene 71-43-2 201.21 182.10 1.0 10.5%
Carbon tetrachloride 56-23-5 1.20 1.10 1.0 8.7%
Chlorine 7782-50-5 371.86 342.16 100.0 8.7%
Cumene 98-82-8 1,548.24 1,499.66 100.0 3.2%
Ethyl chloride (chloroethane) 75-00-3 24.18 24.90 10.0 -2.9%
Ethylene dichloride(1,2-dichloroethane) 107-06-2 T37.07 38.17 1.0
10/15/2015 Page 2 of 4

Facility Total CY 2014 Emission Summary Recorded in ED Facility ID #: 1900039
Facility Name: Moncure Plywood Permit#(s): 03424T24
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants(TAPs) (Pounds/Year)
Pollutant CAS, CY 2014 CY 2013 Demini- %
from ED from Fees mus Change
Formaldehyde 50-00-0 2,632.68 2,354.13 10.0 .1.1.8%
Hexachlorodibenzo-p-dioxin 1,2,3,6,7,8 57653-85-7 0.753130 0.692980 0.0000 8.7%
Hydrogen chloride (hydrochloric acid) 7647-01-0 162.86 149.86 100.0 8.7%
MEK(methyl ethyl ketone, 2-butanone) 78-93-3 108.39 121.89 100.0 -11.1%
Methanol (methyl alcohol) 67-56-1 16,638.61 8,461.97 1,OOO.0 96.6%
Methyl bromide (bromomethane) 74-83-9 61.14 59.23 1.0 3.2%
Methyl chloride (chloromethane) 74-87-3 12.52 11.52 1.0 8.7%
Methylene chloride 75-09-2 54.79 53.07 1.0 3.2%
MIBK(methyl isobutyl ketone) 108-10-1 186.71 184.87 10.0 1.0%
Phenol 108-95-2 1,712.83 1,742.00 100.0 -1.7%
Phosphorus Metal,Yellow or White 7723-14-0 2,565.36 2,360.46 1.0 8.7%
Polycyclic Organic Matter(Inc PAH, dioxins,-etc.N pom 10.51 9.67 1.0 8.7%
&AP 42 historic)
Propionaldehyde 123-38-6 74.81 79.19 10.0 -5.5%
Trichlorobenzene, 1,2,4- 120-82-1 116.91 113.25 100.0 3.2%
Vinyl chloride 75-01-4 40.23 38.97 0.1 3.2%
Vinylidene chloride 75-35-4 60.36 58.64 0.1 2.9%
Xylene (mixed isomers) 1330-20-7 126.21 117.36 100.0 7.5%
Largest Individual HAP Methanol(methyl alcohol) . 16,638.61 lbs
Total HAP Emissions 0,425.19 lbs
10/15/2015 Page 3 of 4

DAQ's Comments Regarding Inventory
Several pollutants have increased/decreased from CY2013 to CY2014(MEK,acrolein,benzene)but the actual emissions have not
changed very much.From CY2013 to CY2014 two pollutants increased significantly,Methanol and Formaldehyde.The change in
emissions is due to two factors(1)Increased production through OS10(2)Stack test data from a December 2014 stack test on OS 10
glue and pressing operations,which changed the emissions factors for that OS that lead to the increased emissions for those two
pollutants.Stack test was reviewed by Gary Saunders.
10/15/2015 Page 4 of 4

MDLI
Boise Cascade
Moncure Plywood Plant
Moncure Plywood
306 Corinth Rd
P.O.Box 230
Moncure,NC 27559
(919)-542-2311
FAX[phone]
Certified Mail/Return Receipt Request
7013 2250 00001816 5159
June 24, 2015
Patrick Butler
Raleigh Regional Office
1628 Mail Service Center
Raleigh,NC 27699-1628
Per General Conditions 3.X of Title V Permit 03424T24, Moncure Plywood submits our annual Air
Emissions Inventory for 2014. A letter was sent to NCDAQ on March 19, 2015 stating that Chris
Seymour needed to be given signature authority duties. The AEI certification page has not yet been
updated in AERO.
If you have any questions or need additional information, please contact me at(803) 581-9261 or cell
at(803) 374-3564.
Si cerely
7ZY
Brian Van elder
Project& Environmental Manager
Enclosures: (2) 2014 North Carolina Air Emissions Inventories
Cc: Brian Van Gelder—Moncure Plywood

FINAL REPORT
2014 NORTH CAROLINA
AIR EMISSIONS INVENTORY
AM
toll"' d �.
Prepared for:
(9
Boise Cascade
Moncure Plywood
306 Corinth Road
Moncure,North Carolina 27559
Prepared hy:
�LrCom
1600 Perimeter Park Drive, Suite 400
Morrisville,North Carolina 27560
AECOM Project No. 60403277
June 2015

2014 NORTH CAROLINA
AIR EMISSIONS INVENTORY
Prepared for:
(9
Boise Cascade
Moncure Plywood
306 Corinth Road
Moncure,North Carolina 27559
Prepared by:
1600 Perimeter Park Drive, Suite 400
Morrisville,North Carolina 27560
[phone]
AECOM Project No. 60403277
June 2015

i
�TABLE OF CONTENTS
Inventory Certification Letter A
Emission Source & Operating Scenario List B
jList of Emission Sources & Control Devices C
i
Facility Summary D
Emission Source Operating Scenario Forms E
and Calculations
, i
Supporting Data F
i '
j

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
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 Jeffrey Matuszak
This person or one that meets the definition below must sign this certification form.
The official submitting the information must certify that he/she complies with the requirements as specified in Title 15A
NCAC 2Q.0520(b)which references and follows the federal definition.40 CFR Part 70.2 defines a responsible as meaning one
of the following:
1.For a corporation: a president, secretary,treasurer,or vice—president of the corporation in charge of a principal
business function,or any other person who performs similar policy or decision making functions for the overall
operation of one or more manufacturing,production,or operating facilities applying for a or subject to a permit and
either
i.the facilities employ more than 250 persons or have gross annual sales or expenditures exceeding$25
million(in second quarter 1980 dollars); or
ii.the delegation of authority to such representatives is approved in advance by the permitting authority;
2. For partnership or sole propietorship;a general partner or the proprietor,respectively;
3. for a muncipality,state,federal,or other public agency includes the chief executive officer having responsibility for the
overall operations of a principal geographic unit of the agency(e.g.,a Regional Administrator of EPA).
CERTIFICATION STATEMENT:
nLegally Respon iblefi i t after all submissionsr
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:
Printed Name: Chris Seymour
Sign re: K�l4 - Z S- ZOI.T
This form applies to Titl acilities. 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: [e-mail]
Information on this Form cannot he held confidential
COPY of RECORD Date Submitted: 6/23/2015 15:27:21 1

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 SOS 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
burner)HAPS lb/mmBtu, (Softwood)
G 24 ES01—A,ES01—B, Veneer dryers and heat source(wood
ES09,ES10 30 burner)lbs/SF,(Hardwood)
1 Veneer dryers and heat source(wood
burner)HAPS Ib/mmBtu,(Hardwood)
36 Natural Gas start up burner(1
MMBW/hr)
G-25 I-4,I-5 5 Ink and painting operations
G-27 ES14,ES17 20 Woodwaste Transfer(Rechipper)
system
ES-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 15 19 tongue and groove operations
ES 16 9 plywood hog
ES20 18 Vat Operations: Heating of Blocks
4

P
ES21 33 End Sealer Spray Booth
ES22 34 Tongue and Groove Saw
I-1 2 Bark hogging operations
r
I-11 25 Hammer hog truck dump—no controls
1-12 24 Dry Waste truck dump
1-2 3 Core chipping and handling operations
I-3 4 Green veneer hogging operations
t 1-6 6 Plywood surface patching
1-7 7 Maintenance parts washer
I-8 8 Veneer diverter exhaust cyclone
IES—GWS 16 Green wood fuel storage silo
11 250 horsepower diesel—fired water
IES 19 pump
35 250 HP Diesel Fired Water Pump
#2—IES23
it
i
1
5

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 *CS ID GCS 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 spreader
Fluidized bed wood burner
with blending chamber and
ESO1—A dedicated overfire air fan(80.0 CS-1 multicyclone CD02
million Btu/hr heat input
capacity)
Boiler(29.79 million Btu/hr
ESO1—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
ESO4 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 M6 t wood—fired veneer dryer CS-1 multicyclone CD02
ES 10 M�2 t wood—fired veneer dryer CS-1 multicyclone CD02
ES 12 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

r--
i
Cyclone(60 inches in
ES14 Rechip blow hog(green wood CS-12 diameter),Woodwaste transfer cyclone CD18,CD03—WWTC,
only) (154 inches in diameter),Bagfilter CD06
(7,095 square feet of filter area),
ES 15 tongue and groove operations
ES 16 Plywood waste hog CS-3 bagfilter(7,095 square feet of filter CD03—WWTC,CD06
area),dry waste transfer cyclone
Green wood sizing operations Cyclone(60 inches in
diameter),Woodwaste transfer cyclone CD18,CD03—WWTC,
ES17 including sizing screens and CS-12 (154 inches in diameter),Bagfilter CD06
bins (154
square feet of filter area),
'- ES20 Vat operations
ES21 End sealer spray booth
ES22 Tongue and groove saw CS-7 bagfilter(7,095 square feet of filter CD06
(plywood finishing) area)
I-1 Bark hogging operations with
two saws
I-10 green wood veneer stacker No.
2
I-11 hammer hog truck dump
I-12 dry waste truck dump
I-2 Core chipping and handling
I-3 Green veneer hogging
1-4 Logo painting and ink marking
I-5 Logo painting and ink marking
1-6 Plywood surface patching
I-7 Maintenance parts washers
1-8 Veneer diverter exhaust
cyclone
I-9 Veen wood veneer stacker No.
1
IES—GWS Green wood fuel storage silo
Diesel—fired water pump(250
IES 19 Horsepower maximum power
output)for emergency purposes
only
3

Facility Total CY 2014 Emissions Summary
COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
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 2014 2013 % Change
Criteria Pollutants
Actual Emissions Tons/Year
Pollutant CAS 2014 2013 % Change
CO CO 30.06 29.28 2.6639302%
NOx NOx 48.06 44.14 8.880838%
PM TSP TSP 59.89 66.42 -9.831374%
PM 10 PM 10 59.85 66.4 -9.864462%
PM2.5 PM2.5 49.52 55.2 -10.289855%
S02 S02 0.76 .7 1 8.571428%
VOC VOC 71.4 63.3 12.796212% 7j
Hazardous Air Pollutants RAPS and/or Toxic Air Pollutants TAPs
Actual Emissions Pounds/Year
Pollutant I CAS 1 2014 1 2013 1 % Change
Pollutant Grou :Antimon Compounds total mass inc elemental Sp)_Group Sum:0.0
Antimony Unlisted Compounds(Specify SBC-Other 0.0 Not reported N/A
Component of SBC
Pollutant Group:Arsenic Compounds(total mass of elemental AS,arsine and all inorganic compounds) Group
Sum:1.51571
Arsenic Unlisted Compounds(Specify ASC-Other 1.51571 1.39462 8.682656%
Component of ASC
Pollutant Group:Beryllium compounds Total mass Group Su :0.0
Beryllium Compound,Unlisted(Specify BEC-Other 0.0 Not reported N/A
Component of BEC
Beryllium metal(unreacted)(Component of
7440-41-7 0.0 Not reported N/A
BEC) I
Pollutant Grou :Cadmium compounds total mass inc elemental metal Group Sum:2.24073
Cadmium Metal(elemental unreacted, 7440-43-9 2.24057 2.06161 8.680598%
Component of CDC
76

Cadmium Unlisted Compounds(Specify T ICDC-Other 1.6E-4 Not reported N/A
Com onent of CDC
Pollutant Group:Chlorinated Dioxin Com ounds of interest as HAP or TAP Grou Sum- 75313
Hexachlorodibenzo-p-dioxin 1,2,3,6,7,8 57653-85-7 0.75313 .69298 8.679908%
r (Component of CLDC
Pollutant Grou :Chromium I Soluble Chromate Compounds (Component of CRC Group Sum:3.28084
Chromic acid(VI) (Component of So1CR6 7738-94-5 3.28084 3.01879 8.680627%
CRC
Pollutant Grou :Chromium-All/Total Inc Chromium categories,metal and Others Group Sum:14.57805
Chromic acid(VI)(Component of SolCR6 7738-94-5 3.28084 3.01879 8.680627%
CRC
L ! Chromium Unlisted Compounds(Specify CRC-Other 11.29721 10.39469 8.682511%
Component of CRC
i� Pollutant Grou :Cobalt compounds Grou Sum:0.0
Cobalt Unlisted Compound(Specify COC-Other 0.0 Not reported N/A
Component of COC
rPollutant Grou :Lead and Lead compounds Group Sum:7.24898
Lead Unlisted Compounds (Specify and PBC-Other 7.24898 6.66993 8.681501%
Component of PBC
Pollutant Grou :Man anese compounds Group Sum:1172.06298
Manganese Unlisted Compounds(Specify
_ MNC-Other 1172.063 1078.44888 8.680443%
Component of MNC)
Pollutant Group:Mercury Compounds-all total mass inc Hg Va or Group Sum:.54171
Mercury Unlisted Compounds (Specify HGC-Other 0.0 Not reported N/A
Component of HGC
Mercury,vapor(Component of HGC 7439-97-6 0.54171 .49808 8.759644%
Pollutant Grou :Nickel Compounds,sum total mass inc elemental Group Sum:5.50759
Nickel Unlisted Compounds (Specify NIC-Other 3.1E-4 Not reported N/A
Component of NIC p
Nickel metal(Component of NIC 7440-02-0 5.50728 5.06741 8.680368%
Pollutant Grou :Pol c clic Organic Matter 7 PAH Compounds for NIF Group Sum:0.0
Benzo(a)pyrene(Component of POMTV 50-32-8 0.0 Not reported N/A
POM7
- Pollutant Grou :Pol c chc Organic Matter(Specific Compounds from OA PS for TV Group Sum:3.83579
Benzo(a)pyrene(Component of POMTV 50-32-8 0.0 Not reported N/A
- POM7
Naphthalene(Component of POMT 91-20-3 3.83579 3.52816 8.719271%
Acetaldehyde 75-07-0 2194.4165 2352.32029 -6.712683%
Acrolein 107-02-8 382.95474 342.27923 11.88372%
Benzene 71-43-2 201.21155 182.10375 10.492811%
Butadiene 1 3- 106-99-0 0.0 Not reported N/A
Carbon tetrachloride 56-23-5 1.20031 1.10444 8.680419%
Chlorine 7782-50-5 371.8593 342.15848 8.680432%
Chlorobenzene 108-90-7 0.0 Not reported N/A
Chloroform 67-66-3 0.0 Not reported N/A
Cumene 98-82-8 1548.24 1499.66315 3.2391794%
Ethyl benzene 100-41-4 0.0 Not reported N/A
Ethyl chloride chloroethane 75-00-3 24.177 24.89575 -2.887039%
Ethylene dichloride 1 2-dichloroethane 107-06-2 37.068 38.17047 -2.8882809%
�i Fluorides sum of all fluoride compounds) 16984-48-8 0.0 Not reported N/A
77

i
Formaldehyde 50-00-0 2632.681 2354.1279 11.832533%
1-7 Hydrogen chloride(hydrochloric acid 7647-01-0 162.86496 149.85675 8.680429%
Methanol 67-56-1 16638.61 8461.96687 96.62816%
Methyl bromide 74-83-9 61.143 59.22956 3.2305503%
Methyl chloride 74-87-3 12.52083 11.52078 8.680407%
Methyl ethyl ketone 78-93-3 108.39225 121.89227 -11.075373%
Methyl isobutyl ketone 108-10-1 186.7112 184.86907 0.99645257%
i
Methylene chloride 75-09-2 54.789 53.06976 3.239589%
Phenol 108-95-2 1712.8289 1741.99891 -1.6745156%
Phosphorus Metal,Yellow or White 7723-14-0 2565.3586 2360.4604 8.680433%
Polycyclic Organic Matter(Inc PAH,
dioxins,etc.NC AP 42 historic amorphous POM 10.51284 9.6722 8.691301%
lob
Pro ionaldeh de 123-38-6 74.80641 79.18664 -5.531522%
Selenium Compounds SEC 0.0 Not reported N/A
Styrene 100-42-5 0.0 Not reported N/A
Toluene 108-88-3 0.0 Not reported N/A
Trichlorobenzene, 1,2,4- 120-82-1 116.91 113.25191 3.2300527%
Trichloroethane, 1,1,2- 79-00-5 0.0 Not reported N/A
Trichloroeth lene 79-01-6 0.0 Not reported N/A
Vinyl chloride 75-01-4 40.23 38.96717 3.2407506%
Vin lidene chloride 75-35-4 60.363 58.64297 2.9330504%
X lene 1330-20-7 126.20702 117.35508 7.5428724%
X lene o- 95-47-6 0.0 Not reported N/A
78

Boise Cascade-Moncure Plywood
Facility-Wide Summary of Actual Emissions
2014 Air Emissions Inventory
1 IM& Dtn A%rite Sander,Fencer IJammer Ilog Drr N1aste
Compound Dryers Storage Systen Stackers I ruck Dump I ruck Dump Emissions Emissions
Ittsl ES-I910 ES-12 ES-O4�-IN-9&10 IS 1A-II 11-P,12 Ib/rr tuns/ r
CO 30.02 60127 30.06
NOx 47.85 96120 48.06
M 31.85 0.55 0.001 0 5' 0.00 0.00 119,797 59.90
PMIU 31_85 0.55 0.001 0 5' 0.00 0.00 119,715 1 59.86
M2.5 31.21 0.55 0.001 0.00 0.00 99042 49.52
VOC 50.38 0.009 142,826 71.41
S02 0.75 1,525 0.76
Compound Emissions oeMinimm Report in
(lb/yr) Ib/yr (Ih1yr) AEV
Acetaldehyde(TH) 1 1,194.41 10 Yes
ceto henone(H) 0.87 100 No
crolein T ;s 382.95 10 Yes
Antimony&Compounds H ; 1.63 10 No
Arsenic&Compounds >' 1.52 0.01 1 Yes
Benzene 'f,I 14 201.23 1 Yes
enzo a ene T 1 1 0.01 1 No
Beryllium Compounds(TH) II W 002 1 No
Cadmium Compounds '3J 2.24 0.1 Yes
Carbon tetrachloride 1 21) 1.20 1 Yes
Chlorine T 371.86 371.86 100 Yes
C'hlorobenzene T 7.81 7.81 10 No
Chloroform(TH) 1.20 1 1.20 100 No
Chromium--Other com 11.30 11.30 0.1 Yc>
Chromium VICompounds(TH) 3.28 3.28 0.01 1r.
Cobalt compounds H 1.00 1.00 1 No
umene 1547.85 1,547.85 100 Yes
initro henol,2,4 0.06 0.06 0.1 No
i 2-eth Ihex I hthalate DEHP) TM 002 0.02 10 No
th 1 benzene(H) I 1 ; 14.73 100 No
th l chloride chloroethane 24.14 24.14 10 Yes
th iene dichloride 37.02 37.02 1 Yes
ormaldeh de T 2041.85 0 14 2,632.68 10 Yes
exachlorodibenzo- oxin 1,2,3,E 7 8 T 0.75 0.75 0.00001 Yes
Hexane(TH) 2.68 2.68 100 No
dro en chloride 162.86 162.86 100 Yes
ead and Lead compounds H) 7.25 7.25 1 Yes
Manganese&compounds(TH) 1 172.06 1,172.06 10 Yes
Mercury Compound(TH) 0.54 0.54 0.001 Yes
Methanol 284652 16 638.60 1000 Yes
Methyl bromide 61.11 61.11 1 Yes
Methyl chloride 12.52 12.52 1 Yes
Methyl chloroform TH 18.50 18.50 100 No
Methyl ethyl ketone T 79,59 108.20 100 Yes
Methyl lsobutyl Ketone TH 157.89 186.67 10 Yes
Methylene di hen 1 diisocyanate(MDD(IT) 0.00 10 No
Methylene chloride T 54.74 54.74 1 Yes
Naphthalene H 3.83 3.84 1 Yes
Nickel Compounds TH 5.51 5.51 1 Yes
Nitro phenol,4- H 0.04 0.04 1 n No
entachloro henol TH 0.02 0.02 1 No
erchloroeth iene T 11.58 11.58 I No
Phenol TH 301.25 1713.02 Ilia Yes
Phosphorus Metal Yellow or White 2565.35 2,565.35 Yes
Polychlorinated bi hen Is (TH) 0.00 0.00 10 No
of c clic Organic Matter H 10.50 10.51 1 Yes
o ionaldeh de H 74.77 74.77 10 Yes
Propylene dichloride H 7.91 7.91 10 No
Selenium compounds H 0.25 0.25 10 No
Styrene 33.05 33.05 100 No
Tetrachlorodibe oxin 2 3 7 8- T 0.00 1 0.00 0.00001 No
Toluene T 27.38 27.42 100 No
Trichlorobenzene 1 2 4- 116.97 116.97 100 Yes'
Trichloroeth iene TH 9.37 9.37 1000 No
Trichlorotluoromethane CFC 111 T) 7.48 7.48 100 No
Trichloro henol 2,4,6 H 0.13 0.13 1 No
Vinyl acetate H 6.70 100 No
Vin 1 chloride 40 26 40.26 0 1 YO s
Vin Iiden oridee chl (l,l-dichloroethene)(TH) 60.40 60.40
X leneITI11 126 14 126.17 100

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
1. Emission Source ID(from permit)or Group GR2 consisting of I-10,I-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 2014: 162377 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 in ermit
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—Fug4 FUGITIVE(NO 1 727 1 Area= 1 Stackers
STACK
6

Operating Scenario: OS—32 Emission Source/Group ID: GR2
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
Hours per Da 24 Days per Week 7 Weeks per Year 52
P Y ( ) Y P ( ) P ( )
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"�u une—Aug. 25% �014
ept.—Nov. 25%
014 014 �014
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
2014
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAAQS) Code Pollutants Method Code (Net after Factor Ef Control
{
�l Pollutants (Tons/Year) (See Instructions) all controls)
2014
CO CO 08
NOx NOx 08
TSP TSP 0.57 08
n
PM10 PM10 0.57 08
PM2.5 PM2.5 08
S02 S02 08
_i
VOC VOC 08
Emission
HAP/TAP Estimation Emissions Control
CAS Emission
Pollutants (In HAP/TAPS Efficiency EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) See Instructions) (Net after all controls)
2014
Ii
r.
I �
11
7

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
1. Emission Source ID(from permit)or Group G-24 consisting of ESO1—A,ES01—B,ES09,ES10
Emission Source Group ID
2. Emission Source Description: Veneer dryers and heat source(wood burner)
3. Operating Scenario ID/Description: OS—26/Veneer dryers and heat source(wood burner)lbs/SF,(Softwood)
4. SCC Number/Description: 30700740/Plywood Operations ;Direct Wood—Fired Dryer:Non—specified
Pine Species Veneer
5. Throughput/units in 2014: 51000000 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 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 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
09cool VERTICAL STACK 46 4 107 35 26389.37 Veneer dryer erp
10A IVERTICAL STACK 66 1 350 155 7304.2 Veneer dryer erp
lOB IVERTICAL STACK 66 1 370 100 4712.38 Veneer dryer erp
10C IVERTICAL STACK 66 1 340 150 7068.58 Veneer dryer erp
8

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
1. Emission Source ID(from permit)or Group G-24 consisting of ESO1—A,ESOl—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—27/Veneer dryers and heat source(wood burner) HAPS ]b/mmBtu,
(Softwood)
4. SCC Number/Description: 30700740/Plywood Operations ;Direct Wood—Fired Dryer:Non—specified
Pine Species Veneer
5. Throughputtunits in 2014: 186094 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#): (r) (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
09cool VERTICAL STACK 46 4 107 35 26389.37 Veneer dryer erp
10A IVERTICAL STACK 66 1 1 350 155 7304.2 Veneer dryer erp
lOB VERTICAL STACK 66 1 370 100 4712.38 Veneer dryer erpd
12

Operating Scenario: OS—27 Emission Source/Group ID: G-24
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
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 Tarch—Ma une—Au . S
ept.—Nov.
�.r 014 25% 014 y 25% �014 g 25% 25%
13. Actual Emissions per Pollutant Listed
I Attach calculations and documentation of emission factors or other estimation methods used.
Emission
Emissions— Estimation Control
GHG CAS GHG Method Efficiency Emission Ef Control
Pollutants Pollutants Code (Net after Factor
(Tons/Year) (See all controls)
r Instructions
2014
Emission
9 k Criteria Emissions— Estimation Control
Pollutant Criteria Method Efficiency Emission
(NAAQS) Code Pollutants Code (Net after Factor Ef Control
Pollutants
� (Tons/Year) (See all controls)
u
Instructions
2014
� CO CO 08 0
! NOx NOx 18.89 08 0 0.203
TSP TSP 12.59 04 65 AFTER
PM10 PM10 12.59 04 65 AFTER
PM2.5 PM2.5 12.34 04 65 AFTER
S02 S02 0.3 08 0 0.00318 AFTER
j VOC VOC 08 0
Emission
Emissions Estimation Control
HAP/TAP CAS Method Efficiency Emission
Alphabetical Order see instructions HAP/TAPS EF Control
Pollutants (In Al
P ) ( )
(Pounds/Year) Code (Net after all Factor
(See controls)
Instructions
� 2014
Arsenic Unlisted Compounds(Specify ASC—Other 0.59922 08 0 0.00000322 AFTER
Component of ASC
Cadmium Metal(elemental unreacted, 7440-43-9 0.88581 08 0 0.00000476 AFTER
Component of CDC
Carbon tetrachloride 56-23-5 0.47454 08 0 0.00000255 AFTER
S Chlorine 7782-50-5 147.01426 08 0 0.00079 AFTER
Chromic acid(VI)(Component of 7738-94-5 1.29708 08 0 0.00000697 AFTER
SolCR6 CRC
Chromium Unlisted Compounds CRC—Other 4.46626 08 0 0.000024 AFTER
(Specify Component of CRC
14

T Hexachlorodibenzo—p—dioxin 1,2,3,6,7,8
Component of CLDC 57653-85-7 0.29775 08 0 0.0000016 AFTER
Hydrogen chloride(hydrochloric acid 7647-01-0 64.38852 08 0 0.000346 AFTER
Lead Unlisted Compounds(Specify and PBC—Other 2.86585 08 0 0.0000154 AFTER
Component of PBC
Manganese Unlisted Com=—]
MNC—Other 463.37406 08 0 0.00249 AFTER
(Specify Component of
Mercur va or Com onent of HGC 7439-97-6 0.21401 08 0 0.00000115 AFTER
• Methyl chloride 74-87-3 4.9501 08 0 0.0000266 AFTER
Methyl ethyl ketone 78-93-3 1.00305 08 0 0.00000539 AFTER
Methyl isobutyl ketone 108-10-1 82.81183 08 0 0.000445 AFTER
"- Naphthalene(Component of POMT 91-20-3 1.51294 08 0 0.00000813 AFTER
Nickel metal(Component of NIC 7440-02-0 2.1773 08 0 0.0000117 AFTER
Phosphorus Metal Yellow or White 7723-14-0 1014.2123 08 0 0.00545 AFTER
Polycyclic Organic Matter(Inc PAH,
dioxins,etc.NC AP 42 historic POM 4.1499 08 0 0.0000223 AFTER
amorphous lob
Pro ionaldeh de 123-38-6 3.98241 08 0 0.0000214 AFTER
, 1
4F
j
r ;
i
15

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
1. Emission Source ID(from permit)or Group G-24 consisting ofES01—A,ES01-13,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 2014: 78000000 FT2/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) ro
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 ft (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
09cool VERTICAL STACK 46 4 107 35 26389.37 Veneer dryer erp
10A VERTICAL STACK 66 1 350 155 7304.2 Veneer dryer erp
lOB VERTICAL STACK 66 1 370 100 4712.38 Veneer er e
10C VERTICAL STACK 66 1 340 150 7068.58 Veneer dryer erp
16

locool IVERTICAL STACKI 46 1 4 105 1 35 1 26389.37 1 Veneer dryer erp
! �I
J �
, a
�-� 17

r.I
Operating Scenario: OS-30 Emission Source/Group ID: G-24
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
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% 25% une-Aug. 25% �014
ept.-Nov. 25%
014 �arch-May
14 �014
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
CAS Ef Control
i Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
1 -
2014
Criteria Emissions- Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po�QS Code Pollutants Method Code (Net after Factor Ef Control
Pollutantss
(Tons/Year) (See Instructions) all controls)
2014
CO CO 14.66 04 0 0.000376 AFTER
NOx NOx 08 0
TSP TSP 08 65
PM10 PM10 08 65
PM2.5 PM2.5 08 65
S02 S02 08 0
VOC VOC 5.23 04 0 0.000134 AFTER
Emission Control
HAP/TAP Emissions
Pollutants (In Alphabetical CAS HAP/TAPSEstimation Efficiency Emission EF Control
(see instructions) Method Code (Net after all Factor
i Order) (Pounds/Year)
See Instructions controls)
- 2014
Acetaldehyde 75-07-0 407.94 08 0 0.00000523 AFTER
Benzene 71-43-2 22.62 08 0 2.9E-7 AFTER
Cumene 98-82-8 696.54 08 0 0.00000893 AFTER
Ethyl chloride chloroethane 75-00-3 18.72 08 0 2.4E-7 AFTER
Ethylene dichloride 107-06-2 28.704 08 0 3.68E-7 AFTER
12-dichloroethane
Formaldehyde 50-00-0 766.74 04 0 0.00000983 AFTER
Methanol 67-56-1 740.22 08 0 0.00000949 AFTER
r
Methyl bromide 74-83-9 27.534 08 0 3.53E-7 AFTER
Methyl ethyl ketone 78-93-3 78.78 08 0 0.00000101 AFTER
Methyl isobutyl ketone 108-10-1 75.114 08 0 9.63E-7 AFTER
Methylene chloride 75-09-2 1 24.648 1 08 0 3.16E-7 AFTER
'._ Phenol 108-95-2 127.14 08 0 0.00000163 AFTER
r-
18

Pro ionaldeh de 123-38-6 70.824 08 0 9.08E-7 AFTER
Trichlorobenzene 12 4— 120-82-1 52.65 08 0 6.75E-7 AFTER
Vinyl chloride 75-01-4 18.096 08 0 2.32E-7 AFTER
Vin lidene chloride 75-35-4 28.08 08 0 3.6E-7 AFTER
X lene 1330-20-7 30.81 08 0 3.95E-7 AFTER
i
I'
r�
y
i ,
19

10C VERTICAL STACK 66 1 340 150 7068.58 Veneer dryer erp
10coo1 IVERTICAL STACKI 46 1 4 105 1 35 1 26389.37 1 Veneer dryer erp
ram,
i
i
L
i '
Ir ,
21

Operating Scenario: OS-31 Emission Source/Group ID: G-24
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
i 11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an-Feb +Dec arch-May o une-Aug. o Sept.-Nov. o
014 25% 014 25/0 014 25/0 014 25/o
r 13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emission
Emissions- Estimation Control
GHG CAS GHG Method Efficiency Emission Ef Control
Pollutants Pollutants Code (Net after Factor
(Tons/Year) (See all controls)
Instructions
2014
Emission
Criteria Emissions- Estimation Control
Pollutant Criteria Method Efficiency Emission
- (NAAQS) Code Pollutants Code (Net after Factor Ef Control
Pollutants
--� (Tons/Year) (See all controls)
Instructions
2014
CO CO 08 0
NOx NOx 28.89 08 0 0.203 AFTER
TSP TSP 19.25 08 65 AFTER
PM10 PM10 19.25 08 65 AFTER
PM2.5 PM2.5 18.87 08 65 AFTER
S02 S02 0.45 08 0 0.00318 AFTER
VOC VOC 08 0
'-' Emission
Emissions Estimation Control
HAP/TAP CAS Emission
Pollutants (In Alphabetical Order see instructions) Method Efficiency EF Control
�_ P ) ( ) (Pounds/Year) Code (Net after all Factor
(See controls)
Instructions
2014
Acrolein 107-02-8 36.14598 08 0 0.000127 AFTER
Arsenic Unlisted Compounds(Specify ASC-Other 0.91646 08 0 0.00000322 AFTER
Component of ASC
Cadmium Metal(elemental unreacted, 7440-43-9 1.35476 08 0 0.00000476 AFTER
- Component of CDC
Carbon tetrachloride 56-23-5 0.72577 08 0 0.00000255 AFTER
Chlorine 7782-50-5 224.84506 08 0 0.00079 AFTER
Chromic acid(VI) (Component of 7738-94-5 1.98376 08 0 0.00000697 AFTER
So1CR6 CRC
CRC-Other 6.83074 08 0 0.000024 AFTER
22

Chromium Unlisted Compounds
(Specify Component of CRC
Hexachlorodibenzo—p—dioxin 1,2,3,6,7,8 57653-85-7 0.45538 08 0 0.0000016 AFTER
(Component of CLDC
!" Hy dro en chloride(hydrochloric acid 7647-01-0 98.47644 08 0 0.000346 AFTER
Lead Unlisted Compounds (Specify and
PBC—Other 4.38306 08 0 0.0000154 AFTER
Component of PBC
Manganese Unlisted Compounds MNC—Other 708.68886 08 0 0.00249 AFTER
(Specify Component of MNC
Mercury,vapor(Component of HGC 7439-97-6 0.32731 08 0 0.00000115 AFTER
Methyl chloride 74-87-3 7.57073 08 0 0.0000266 AFTER
!. Naphthalene(Component of POMT 91-20-3 2.31391 08 0 0.00000813 AFTER
Nickel metal(Component of NIC 7440-02-0 3.32998 08 0 0.0000117 AFTER
Phosphorus Metal Yellow or White 7723-14-0 1551.1463 08 0 0.00545 AFTER
Polycyclic Organic Matter(Inc PAH,
dioxins,etc.NC AP 42 historic POM 6.34689 08 0 0.0000223 AFTER
amorphous lob
L
23

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
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—36/Natural Gas start up burner(1 MMBtu/hr)
4. SCC Number/Description: Not required by facility,will be completed by DAQ
5. Throughputlunits in 2014: 1.49 E6FT3S/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) ro
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 ft (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
09cool VERTICAL STACK 46 4 107 35 26389.37 Veneer dryer erp
10A VERTICAL STACK 66 1 350 155 7304.2 Veneer drver e
IOB VERTICAL STACK 66 1 370 100 4712.38 Veneer dryer erp
10C VERTICAL STACK 66 1 340 150 7068.58 j Veneer dryer erp
IOcool VERTICAL STACK 46 4 105 35 26389.37 Veneer dryer erp
24

Operating Scenario: OS—36 Emission Source/Group ID: G-24
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
Hours per Day ( 1 ) Days per Week ( 1 ) 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% �014
ept.—Nov. 25%
014 014 �014
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
2014
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po� Code Pollutants Method Code (Net after Factor Ef Control
Pollutants (Tons/Year) (See Instructions) all controls)
L -I` 2014
CO CO 0.06 08 0
NOx NOx 0.07 08 0
TSP TSP 0 08 65
PM10 PM10 0 08 65
PM2.5 PM2.5 0 08 65
L S02 S02 0 08 0
VOC VOC 0 08 0
HAP/TAP Emissions Emission Control
CAS Estimation Efficiency Emission
Pollutants (In Alphabetical ( ) HAP/TAPS Method Code (Net after all Factor EF Control
see instructions)
(Pounds/Year)
See Instructions controls)
2014
Arsenic Unlisted
Compounds(Specify ASC—Other 0.00003 08 .0
— Component of ASC
Benzene 71-43-2 _ 0.0031 08 0
Cadmium Unlisted
`- Compounds (Specify CDC—Other 0.00016 08 0
—Component of CDC
Chromium Unlisted
Compounds (Specify CRC—Other 0.00021 08 0
Component of CRC
Formaldehyde 50-00-0 0.112 08 0
Lead Unlisted Compounds
(Specify and Component of PBC—Other 0.00007 08 0
PBC
MNC—Other 0.00006 08 0
26

Manganese Unlisted
Compounds(Specify
Component of MNC
Mercury,vapor(Component 7439-97-6 0.00039 08 0
} of HGC
Naphthalene(Component of 91-20-3 0.00091 08 0
POMT
Nickel Unlisted Compounds NIC—Other 0.00031 08 0
(Specify Component of NIC
Polycyclic Organic Matter
(Inc PAH,dioxins,etc.NC pOM 0.00013 08 0
AP 42 historic amorphous
lob
i_J
27

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
1. Emission Source ID(from permit)or Group G-25 consisting of I-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 2014: 1275 GAL/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur ro Ash I I 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 ft (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
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
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% 25% une—Aug. 25% �014
ept.—Nov. 25%
014 �arch—May
14 �014
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/Yea See Instructions all controls
2014
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po� Code Pollutants Method Code (Net after Factor Ef Control
Pollutants (Tons/Year) (See Instructions) all controls)
I �
2014
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 0.49 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)
See Instructions
2014
29

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
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 2014: 29341 TON/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-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

Operating Scenario: OS—20 Emission Source/Group ID: G-27
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
F_�
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% �014
ept.—Nov. 25%
014 014 �014
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
I 2014
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po� Code Pollutants Method Code (Net after Factor Ef Control
Pollutants (Tons/Year) (See Instructions) all controls)
2014
CO CO 08 0
NOx NOx 08 0
TSP TSP 0.39 02 99.7 AFTER
PM10 PM10 0.39 02 99.7 AFTER
PM2.5 PM2.5 0.39 02 99.7 AFTER
S02 S02 08 0
VOC VOC 08 0
Emission
HAP/TAP Emissions Control
Pollutants (In CAS HAP/TAPS Estimation Efficiency Factor Emission
(see instructions) Method Code EF Control
_
Alphabetical Order) (Pounds/Year) See Instructions (Net after all controls)
2014
I`-
I
1
31

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
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 2014: 118019000 FT2/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) ro
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)
I 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 ft (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
32

C.
Operating Scenario: OS—21 Emission Source/Group ID:
ES03—SMS-1
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
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 an—Feb +Dec 25% M 25% une—Aug. 25% �014
ept.—Nov. 25%
014 �arch— ay
14 �014
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
2014
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency
Emission
Po� Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2014
CO CO 08 0
NOx NOx 08 0
TSP TSP 12.1 04 85 AFTER
PM10 PM10 12.1 04 85 AFTER
PM2.5 PM2.5 12.1 04 0 AFTER
S02 S02 08 0
{ VOC VOC 08 0
y HAP/TAP CAS Emissions Emission ControlControl Emission
Pollutants (In (see instructions) HAP/TAPS Method Code Efficiency Factor EF Control
I Alphabetical Order) (Pounds/Year) (Net after all controls)
-- See Instructions
2014
II �
33

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
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 2014: 177090 FT2/yr
(e.g. production or fuel use):
6. Fuel Information (If fuel is used) ro 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-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 ilter(7,095 square feet of filter area
9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional ent 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
Fin 0.1 feet)
EP—WS DOWNWARD—FACING VENT 10 1 72 1 47.12 ERP for wood
sander
34

G
Operating Scenario: OS— 12 Emission Source/Group ID: ESO4
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
�r
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec T 25/0 o 25/a arch—May o 25/0 une—Aug. o �014
ept.—Nov. 25/o
o
014 014 �014
13. Actual Emissions per Pollutant Listed
l� 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
r 2014
l Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAAQS) Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
n (Tons/Year) (See Instructions) all controls)
2014
CO CO 08 0
NOx NOx 08 0
TSP TSP 0 04 95 0.0000115 AFTER
PM10 PM10 0 04 95 0.0000115 AFTER
PM2.5 PM2.5 0 04 95 0.0000115 AFTER
S02 S02 08 0
VOC VOC 0.01 08 0 0.000151 AFTER
a Emission Control
HAP/TAP Emission Estimation Efficiency Emission
Pollutants (In see instructions HAP/TAPS EF Control
( )
Alphabetical Order) (Pounds/Year) Method Code (Net after all Factor
See Instructions controls)
2014
Acetaldehyde 75-07-0 0.21 08 0
Formaldehyde 50-00-0 0.14 08 0
Methanol 67-56-1 0.91 08 0
s
i
I '
35

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
1. Emission Source ID(from permit)or ES 12
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 2014: 118019000 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 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 VERTICAL STACK 60 0.7 72 0.45 13.57 silo e
36

n
Operating Scenario: OS— 17 Emission Source/Group ID: ES12
�N 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
it r
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"�o Sept.—Nov. 25%
2014 014 �014 014
13. Actual Emissions per Pollutant Listed
! Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
a�f GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2014
i Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po�QS Code Pollutants Method Code (Net after Factor Ef Control
Pollutantss
�
(Tons/Year) (See Instructions) all controls)
2014
CO CO 08 0
NOx NOx 08 0
TSP TSP 0.55 10 99.9 0.00000929 AFTER
PM10 PM10 0.55 10 99.9 0.00000929 AFTER
I PM2.5 PM2.5 0.55 10 99.9 0.00000929 AFTER
S02 S02 08 0
i
VOC VOC 08 0
tv Emission Control
HAP/TAP Emissions
Pollutants (In CAS HAP/TAPSEstimation Efficiency Emission EF Control
(see instructions) Method Code (Net after all Factor
l Alphabetical Order) (Pounds/Year)
See Instructions controls)
2014
I �
i
iJ
'i + 37

' i
Operating Scenario: OS— 10 Emission Source/Group ID: ES13—GMO
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
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:
r an—Feb +Dec 25% 25% une—Aug. 25% Sept.—Nov. 25%
014 �arch—May
14 �014 014
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
r 2014
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po� Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
+ 2014
CO CO 08
NOx NOx 08
TSP TSP 8.28 08 0.0002
_z
PM10 PM10 8.28 08 0.0002
PM2.5 PM2.5 3.44 08 0.0000832
S02 S02 08
VOC VOC 7.08 08 0.000171
`._ Emission Control
HAP/TAP Emissions
Pollutants (In CAS HAP/TAPSEstimation Efficiency Emission EF Control
(see instructions) Method Code (Net after all Factor
c Alphabetical Order) (Pounds/Year)
See Instructions controls)
2014
Formaldehyde 50-00-0 413.93 08 0.000005
Methanol 67-56-1 9189.246 08 0.000111
-" Phenol 108-95-2 1316.2974 08 0.0000159
I�t
i '
39

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
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. Throughputlunits in 2014: 35233000 FT2/yr
(e.g.production or fuel use):
6. Fuel Information (if fuel is used) /o Sulfur ro Ash I 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 rented 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 Terp for gluing and
erp-13 STACK 3.05 125 Area= ress o erations
40

F,
Operating Scenario: OS—28 Emission Source/Group ID: ES13—GMO
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
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% �014
ept.—Nov. 25%
014 014 �014
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
2014
r
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
��QS) Ef Control
Code Pollutants Method Code (Net after Factor
Pollutants (Tons/Year) (See Instructions) all controls)
2014
CO CO 08
w NOx NOx 08
TSP TSP 3.52 08 0.0002
PM10 PM10 .3.52 08 0.0002
PM2.5 PM2.5 1.47 08 0.0000832
t-` S02 S02 08
VOC VOC 10.34 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)
�-� 2014 See Instructions controls)
Acetaldehyde 75-07-0 127.19113 08 0.00000361
M Formaldeh 08 0.000005
Methanol 67-56-1 3910.863 08 0.000111
Methyl ethyl ketone 78-93-3 28.6092 08 8.12E-7
Methyl isobutyl 108-10-1 28.78536 08 8.17E-7
ketone
Phenol 108-95-2 95.48143 08 0.00000271
41

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
1. Emission Source ID(from permit)or ES 15
Emission Source Group ID
2. Emission Source Description: tongue and groove operations
3. Operating Scenario ID/Description: OS— 19/tongue and groove operations
4. SCC Number/Description: 30700710/Plywood Operations ; Sawing
5. Throughput/units in 2014: 0
(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)
42

Operating Scenario: OS— 19 Emission Source/Group ID: ES15
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
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% 25% une—Aug. 25% �014
ept.—Nov. 25%
014 �arch—May
14 �014
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
V GHG GHG Estimation Efficiency Emission
V CAS Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2014
Emissions— Emission Control
Criteria Pollutant Criteria Estimation Efficiency Emission
Po� Code Pollutants Method Code (Net after Factor Ef Control
Pollutants (Tons/Year) (See Instructions) all controls)
i
2014
rJ
CO CO 08
NOx NOx 08
TSP TSP 08
r,r PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
Emission
HAP/TAP Emissions 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
2014
� I
ti 43

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
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 2014: 93000000 FT2/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) % 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)
I 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 ft (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
7EP-P-20 FUGITIVE(NO 1 100 Area= 1 Vats
STACK
46

Operating Scenario: OS— 18 Emission Source/Group ID: ES20
j 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
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 rarch—Mayune—Aug. o �014
ept.—NOV. °
�014 25% 25% �014 25/0 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
2014
Criteria Emissions— Emission Control
(N �/�/ Pollutant Criteria Estimation Efficiency Emission
Pollutants
�) Code Pollutants Method Code (Net after Factor Ef Control
Poollutants (Tons/Year) (See Instructions) all controls)
2014
CO CO 08
NOx NOx 08
TSP TSP 08
_} PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 1.98 08
Emission Control
ELAP/TAP Emissions
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)
— 2014
Acetaldehyde 75-07-0 434.31 08 0.00000467
Methanol 67-56-1 682.62 08 0.00000734
47

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
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 2014: 2700 GAL/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)
�--1 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 ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
FEP-21 VERTICAL STACK 20 1 70 10 471.23 End Sealer Spray
Booth
48

r
Operating Scenario: OS—33 Emission Source/Group ID: ES21
j 10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
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% 25%25% une—Aug. 25% �014
ept.—Nov. 25%
2014 014 �014
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
j 2014
Criteria Emissions— Emission Control
-- Pollutant Criteria Estimation Efficiency Emission
Po� Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2014
CO CO 08
NOx NOx 08
TSP TSP 0.07 03
PM10 PM10 0.07 03
PM2.5 PM2.5 08
S02 S02 08
y
VOC VOC 0.04 03
HAP/TAP CAS Emissions Emission Estimation Control Emission
Pollutants (In (see instructions) HAP/TAPS Efficiency Factor EF Control
Method Code
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2014
l '
r-,
49

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
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 2014: 1238927 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-7 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-06 VERTICAL STACK 30 2.8 72 50 18472.56 erp for woodwaste
system
50

r-,
Operating Scenario: OS —34 Emission Source/Group ID: ES22
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
Hours per Day ( 3 ) Days per Week ( 1 ) Weeks per Year ( 35 )
17
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% �014
ept.—Nov. 25%
014 014 014
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
CAS Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2014
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)
2014
CO CO 08 0
NOx NOx 08 0
TSP TSP 0.04 02 99.5
PM10 PM10 0.01 02 99.5
PM2.5 PM2.5 0.01 08 99.5
` S02 S02 08 0
VOC VOC 0.05 08 0 0.0000755 AFTER
Emission Control
HAP/TAP Emissions
Pollutants (In CAS HAP/TAPSEstimation Efficiency Emission EF Control
(see instructions) Method Code (Net after all Factor
Alphabetical Order) (Pounds/Year) See Instructions controls)
2014
Acetaldehyde 75-07-0 0.69256 08 0 5.59E-7 AFTER
Formaldehyde 50-00-0 0.48194 08 0 3.89E-7 AFTER
Methanol 67-56-1 8.44948 08 0 0.00000682 AFTER
i
L_
�i
51

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
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 2014: 20584 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 entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter ft (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
52

Operating Scenario: OS—2 Emission Source/Group ID: I-1
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
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% 25% une—Aug. 25% �014
ept.—Nov. 25%
2014 �arch—May
14 �014
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
2014
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po� Code Pollutants Method Code (Net after Factor Ef Control
Pollutants (Tons/Year) (See Instructions) all controls)
2014
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
CAS Estimation Emission
Pollutants (In (see instructions) HAP/TAPS Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2014
I ,
L I
53

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
1. Emission Source ID (from permit)or I-11
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 2014: 2006 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)
F
P—Fug3 FUGITIVE(NO 1 72 Area— 1 Hammer Hog Truck
STACK) Dump
54

I ^,
Operating Scenario: OS—25 Emission Source/Group ID: I-11
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
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. 250�o �014
ept.—Nov. 25%
014 014 �014
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 Ef Control
Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
�1 2014
Emissions— Emission Control
Criteria pollutant Criteria Estimation Efficiency Emission
Po� Code Pollutants Method Code (Net after Factor Ef Control
Pollutants (Tons/Year) (See Instructions) all controls)
L 2014
CO CO 08
NOx NOx 08
- TSP TSP 0 08 0.0000396
_ PM10 PM10 0 08 0.0000187
PM2.5 PM2.5 0 08 0.00000283
S02 S02 08
VOC VOC 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)
- 2014
I
55

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
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 2014: 944 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 Arca - 1 Dry Waste Truck
STACK Dump
56

Operating Scenario: OS—24 Emission Source/Group ID: I-12
10'.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
j11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
i an—Feb +Dec 25% 25% une—Aug. 25% �014
ept.—Nov. 25%
014 �arch_-May
14 �014
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
2014
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)
2014
CO CO 08
NOx NOx 08
TSP TSP 0 08 0.0000396
PM10 PM10 0 08 0.0000187
PM2.5 PM2.5 0 08 0.00000283
S02 S02 08
VOC VOC 08
- Emission Control
HAP/TAP Emissions
Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code (Net after all Factor
Alphabetical Order) (Pounds/Year)
C See Instructions controls)
2014
I
57

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
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 2014: 241 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 in ennit
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)
FEP—FUG FUGITIVE(NO 1 72 Area= 1 ERP for Fugitive
STACK) sources
58

I
er Scenario: OS—3 Emission Source/Grow ID: I-2
Operating Sce p
I�l
f 10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
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 250�o une—Aug. 25"�o �014
ept.—Nov. 25%
014 014 �014
13. Actual Emissions per Pollutant Listed
i1 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
ji 2014
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
��QS) Ef Control
Code Pollutants Method Code (Net after Factor
Pollutants (Tons/Year) (See Instructions) all controls)
2014
CO CO 08
NOx NOx 08
TSP TSP 0 08 0.024
PM10 PM10 0 08 0.011
{ ! PM2.5 PM2.5 0 08 0.0046
S02 S02 08
VOC VOC 08
!-_ HAP/TAP Emissions Emission Control
Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Factor
Alphabetical Order) (Pounds/Year) Method Code (Net after all controls)
See Instructions
2014
p
; n
59

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
1. Emission Source ID(from permit)or I-3
Emission Source Group ID
2. Emission Source Description: Green veneer hogging
3. Operating Scenario ID/Description: OS —4/Green veneer hogging operations
4. SCC Number/Description: 30700799/Plywood Operations ; Other Not Classified
5. Throughput/units in 2014: 29100 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— 1 ERP for Fugitive
STACK) sources
60

I
Operating Scenario: OS—4 Emission Source/Group ID: I-3
k
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
I
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +D ec 014 �014 arch—Ma une—Au Sept.—Nov.014o25% y 25% g' 25% 25/o014
13. Actual Emissions per Pollutant Listed :
+ Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
k GHG GHG Estimation Efficiency Emission
Pollutants CAS Ef Control
Pollutants Method Code (Net after Factor
Tons/Yea See Instructions all controls
2014
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAAQS) Code Pollutants Method Code (Net after Factor Ef Control
1 Pollutants (Tons/Year) (See Instructions) all controls)
2014
CO CO 08
NOx NOx 08
TSP TSP 0.02 08
PM10 PM10 0.01 08
� t PM2.5 PM2.5 0 08
V
S702 S02 08
OC VOC 08
Emission
HAP/TAP CAS Emissions Estimation Control Emission
Pollutants (In (see instructions) HAP/TAPS Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) See Instructions) (Net after all controls)
2014
i �
�n
61

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
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 2014: 22316 GAL/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 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 ft (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

Operating Scenario: OS—6 Emission Source/Group ID: I-6
7-1
` 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
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% 25%25% une—Aug. 25% �014
ept.—Nov. 25%
014 014 �014
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
k GHG CAS GHG Estimation Efficiency Emission Ef Control
? Pollutants Pollutants Method Code (Net after Factor
Tons/Yea See Instructions all controls
2014
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAAQS) Code Pollutants Method Code (Net after Factor Ef Control
r Pollutants
� (Tons/Year) (See Instructions) all controls)
2014
CO CO 08
NOz NOz 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
` S02 S02 08
VOC VOC 0.64 03
HAP/TAP Emissions Emission Control
s 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
- 2014
r�
f
I
I
I
63

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
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. Throughputlunits in 2014: 110 GAL/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 ft (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
64

�l
Operating Scenario: OS—7 Emission Source/Group ID: I-7
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
j 11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec une—Au . S
ept.—Nov. 25/o
014 25% �arch—May
14 25% �014 g 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/Year See Instructions all controls
i 2014
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)
2014
CO CO 08
NOz NOz 08
~ TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 0.39 03 7
Emission
HAP/TAP Emissions 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)
`- 2014
65

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
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 2014: 162377 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 ft (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
66

Operating Scenario: OS—8 Emission Source/Group ID: I-8
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
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% �014
ept.—Nov. 25%
2014 014 �014
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
2014
Criteria Emissions— Emission Control
- (NAAQS) Pollutant Criteria Estimation Efficiency Emission Ef Control
Pollutants Code Pollutants Method Code (Net after Factor
i (Tons/Year) (See Instructions) all controls)
2014
CO CO 08
NOx NOx 08
TSP TSP 2.15 02
PM10 PM10 2.15 02
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
�-- HAP/TAP Emissions Emission Control
CAS Estimation Emission
Pollutants (In (see instructions) HAP/TAPS Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2014
i
' r
' f
i
67

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
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 2014: 20584 TON/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sul llir 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 ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x
(in 0.1 feet)
e l 1.1 DOWNWARD—FACING VENT 70 1.25 72 0.45 33.13 silo vent
e l l.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 1 l.4 DOWNWARD—FACING VENT 1 70 1.25 72 0.45 33.13 silo vent
68

r
T Operating Scenario: OS— 16 Emission Source/Group ID: IES—GWS
j 10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
_ 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 une—Aug. ° �014
ept.—Nov. °
2014 25% �arch_-May
14 25% �014 25/° 25/°
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
2014
Criteria Emissions— Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission Ef Control
Code Pollutants Method Code (Net after Factor
Pollutants (Tons/Year) (See Instructions) all controls)
2014
CO CO 08
NOx NOx 08
� TSP TSP 0 08 0.0000396
_ PM10 PM10 0 08 0.0000187
' ? PM2.5 PM2.5 0 08 0.00000283
S02 S02 08
I` VOC VOC 08
PEmission Control
1 HAP/TAP Emissions
Pollutants (In CAS HAP/TAPSEstimation Efficiency Emission EF Control
(see instructions) Method Code (Net after all Factor
,f Alphabetical Order) (Pounds/Year)
See Instructions controls)
2014
I
i.
i
it
I i
�i
li
69

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
1. Emission Source ID(from permit)or IES19
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 2014: 84.6 E6BTU/yr
(e.g.production or fuel use):
6. Fuel Information (if fuel is used) /o Sulfur 0.002 ro
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 ft (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
70

rr
Operating Scenario: OS- 11 Emission Source/Group ID: IES 19
j10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
Hours per Day ( 3 ) Days per Week ( 1 ) Weeks per Year ( 44 )
C11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an-Feb +Dec 25a/o Farch-May 250�o une-Aug. 250�o �014
ept.-Nov. 25"�0
2014 014
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
l- -
Emissions- Emission Control
GHG GHG Estimation Efficiency Emission
Pollutants CAS Pollutants Method Code (Net after Factor Ef Control
Tons/Year See Instructions all controls
2014
Emissions- Emission Control
Criteria Pollutant Criteria Estimation Efficiency Emission
��QS) Ef Control
Code Pollutants Method Code (Net after Factor
Pollutants (Tons/Year) (See Instructions) all controls)
i
' 2014
CO CO 0.04 08 0.95
NOx NOx 0.19 08 4.41
TSP TSP 0.01 08 0.31
PM10 PM10 0.01 08 0.31
j PM2.5 PM2.5 0.01 08 0.31
S02 S02 0.01 08 0.29
VOC VOC 0.01 08 0.35
Emission Control
HAP/TAP CAS Emissions Estimation Efficiency enc y Emission EF Control
Pollutants (In Alphabetical Order) (see instructions) Method Code (Net after all Factor
(Pounds/Year)
See Instructions controls)
L 2014
Acetaldehyde 75-07-0 0.06489 08 0.000767
Acrolein 107-02-8 0.00783 08 0.0000925
Benzene 71-43-2 0.07893 08 0.000933
Formaldehyde 50-00-0 0.09983 08 0.00118
i Naphthalene(Component of POMT 91-20-3 0.00717 08 0.0000848
Polycyclic Organic Matter
(Inc PAH,dioxins,etc.NC POM 0.01421 08 0.0001.68
AP 42 historic amorphous
t - lob
X lene 1330-20-7 0.02411 08 0.000285
71

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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 2014
1. Emission Source ID(from permit)or IES19
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: 2020040 1/Diesel; Diesel
5. Throughput/units in 2014: 10.2 E6BTU/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) ro
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 ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
e rp—wp VERTICAL STACK 8 0.42 72 1 8.31 erp for diesel—fired
water um
73

1
Operating Scenario: OS—35 Emission Source/Group ID: IES 19
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
Hours per Day ( 1 ) Days per Week ( 1 ) Weeks per Year ( 16 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
5� 14 g. 25% S
ept.—Nov.+Dec arch—May une—Au
�014 2 0 25% �014 25/
13. Actual Emissions per Pollutant Listed
j 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
2014
Criteria Emissions— Emission Control
- S Pollutant Criteria Estimation Efficiency Emission
AAQ Ef Control
Pollutant Code Pollutants Method Code (Net after Factor
(Tons/Year) (See Instructions) all controls)
2014
CO CO 0 08 0.95
NOx NOx 0.02 08 4.41
TSP TSP 0 08 0.31
PM10 PM10 0 08 0.31
PM2.5 PM2.5 0 08 0.31
` S02 S02 0 08 0.29
VOC VOC 0 08 0.35
Emissions Emission Control
HAP/TAP CAS Estimation Efficiency Emission
Pollutants (In Alphabetical Order) (see instructions) HAP/TAPS(Pounds/Year) Method Code (Net after all Factor EF Control
�
See Instructions controls)
2014
Acetaldehyde 75-07-0 0.00782 08 0.000767
Acrolein 107-02-8 0.00094 08 0.0000925
Benzene 71-43-2 0.00952 08 0.000933
Formaldehyde 50-00-0 0.01204 08 0.00118
Naphthalene(Component of POMT 91-20-3 0.00086 08 0.0000848
Polycyclic Organic Matter
— (Inc PAH,dioxins,etc.NC pOM 0.00171 08 0.000168
AP 42 historic amorphous
lob
X lene 1330-20-7 0.00291 08 0.000285
4
74

Boise Cascade-Moncure Plywood Z9
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
2014 Actual Process Throughput: 7,666 Boiler operating hours/yr
42,098 ton wood/yr
470,707 MMBtu/yr Total Fuel Combusted
272,004 MMBtu/yr Green Wood Combusted
198,703 MMBtu/yr Dry Wood Combusted
78,000,000 sf/yr Hardwood Veneer Production
51,000,000 sf/yr Softwood Veneer Production
129,000,000 sf/yr Total Veneer Production
284,614 MMBtu/yr Btu of Wood Combusted-ratioed for Hardwood Veneer
186,094 MMBtu/yr Btu of Wood Combusted-ratioed Softwood Veneer
Actual Emissions Summary: \� 0
Hardwood vSoftwood Total
Compound Emission Factor Units Ref. Emissions* Emission Factor Units Ref. Emissions* Emissions
ton/ r ton/ r ton/ r
CO 3.76E-04 lb/sf 1 14.66 6.00E-04 lb/sf 1 15.30 30.0
Ox 2.03E-01 lb/MMBtu 6 28.89 2.03E-01 lb/MMBtu 6 18.89 47.8
PM 8.308 lb/hr 3 19.25 8.308 lb/hr 3 12.59 - 31.8
PM10 8.308 lb/hr 3 19.25 8.308 lb/hr 3 12.59 31.8
PM2.5 8.14 lb/hr 3 18.87 8.14 lb/hr 3 12.34 31.2
VOC as acetic acid-hardwood and pinene-softwood 2.41E_04 lb/sf 1 9.41 1.07E-03 lb/sf 1 27.29 36.7
WPP1 VOC 1.34E-04 lb/sf 4 5.24 1.77E-03 lb/sf 4 45.14 50.4
SO2 3.18E-03 lb/MMBtu 6 0.45 3.18E-03 lb/MMBtu 6 0.30 0.75
Compound Emission Factor Units Ref. lb/ r Emissions* Emission Factor Units Ref. Emissions* Emissions
Ib/ r lb/ r
Acetaldehyde(TH) 5.23E-06 lb/sf 2 407.94 2.40E-05 lb/sf 2 1224.00 1631.94
Aceto henone H 1.84E-06 lb/MMBtu 6 0.52 1.84E-06 lb/MMBtu 6 0.34 0.87
Acrolein TH 1.27E-04 lb/MMBtu 6 36.15 6.80E-06 lb/sf 2 346.80 382.95
Antimony&compounds H 3.46E-06 lb/MMBtu 6 0.98 3.46E-06 lb/MMBtu 6 0.64 1.63
Arsenic&compounds TH 3.22E-06 lb/MMBtu 6 0.92 3.22E-06 lb/MMBtu 6 0.60 1.52
Benzene TH 2.90E-07 lb/sf 2,7 22.64 3.50E-06 lb/sf 2 178.50 201.14
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 0.01 0.02
Cadmium&compounds(TH) 4.76E-06 lb/MMBtu 6 1.35 4.76E-06 lb/MMBtu 6 0.89 2.24
Carbon tetrachloride TH 2.55E-06 lb/MMBtu 6 0.73 2.55E-06 lb/MMBtu 6 0.47 1.20
Chlorine TH 7.90E-04 lb/MMBtu 5 224.84 7.90E-04 lb/MMBtu 5 147.01 371.86
Chlorobenzene TH 1.66E-05 lb/MMBtu 6 4.72 1.66E-05 lb/MMBtu 6 3.09 - 7.81

i
t
Cr
Boise Cascade-Moncure Plywood rvv r
Emission Source(s): Fluidized Bed Wood Boiler and Two Direct Heated Dryers V^
Source ID Number(s):ES-01,ES-09,ES-10,CD-02(multiclone on boiler)
Emission Point(s): EP-09a-d,EP-10a-d - U
2014 Actual Process Throughput: 7,666 Boiler operating hours/yr Q �ilj®
� \
42,098 ton wood/yr 0 �®�
470,707 MMBtu/yr Total Fuel Combusted
272,004 MMBtu/yr Green Wood Combusted
198,703 MMBtu/yr Dry Wood Combusted
78,000,000 sf/yr Hardwood Veneer Production
51,000,000 sf/yr Softwood Veneer Production
129,000,000 sf/yr Total Veneer Production
284,614 MMBtu/yr Btu of Wood Combusted-ratioed for Hardwood Veneer
186,094 MMBtu/yr Btu of Wood Combusted-ratioed for Softwood Veneer
Actual Emissions Summary:
Hardwood Softwood Total
Compound Emission Factor Units Ref. lb/ r Emissions* Emission Factor Units Ref. Emissions* Emissions*
lb/ r Ib/ r
Chloroform TH 2.55E-06 Ib/MMBtu 6 0.73 2.55E-06 lb/MMBtu 6 0.47 1.20
Chromium compounds H 2.40E-05 Ib/MMBtu 6 6.83 2.40E-05 lb/MMBtu 6 4.47 11.30
Chromium VI T/H 6.97E-06 lb/MMBtu 6 1.98 6.97E-06 lb/MMBtu 6 1.30 3.28
Cobalt compounds H 2.12E-06 lb/MMBtu 6 0.60 2.12E-06 lb/MMBtu 6 0.39 1.00
Cumene(H) 8.93E-06 lb/sf 2,7 696.15 1.67E-05 Ib/sf 2,7 851.70 1547.85
Dinitro henol,2,4- H 1.31E-07 lb/MMBtu 6 0.04 1.31E-07 lb/N4MBtu 6 0.02 0.062
Di(2-eth ]hex 1) hthalate DEHP TH 4.65E-08 lb/MMBtu 6 0.01 4.65E-08 lb/MMBtu 6 0.01 0.022
Ethyl benzene H) 3.13E-05 lb/MMBtu 6 8.91 3.13E-05 lb/MMBtu 6 5.82 14.73
Ethyl chloride chloroethane) H) 2.40E-07 lb/sf 2,7 18.70 1.07E-07 lb/sf 2,7 5.44 24.14
Ethylene dichloride 1,2-dichloroethane)(TH) 3.68E-07 lb/sf 2,7 28.67 1.64E-07 Ib/sf 2,7 8.35 37.02
Formaldehyde(TH) 9.83E-06 lb/sf 1 766.74 2.50E-05 lb/sf 1 1275.00 2041.74
Hexachlorodibenzo- -dioxin 1,2,3,6,7,8 T) 1.60E-06 lb/MMBtu 5 0.46 1.60E-06 lb/MMBtu 5 0.30 0.75
Hydrogen chloride hydrochloric acid (TH) 3.46E-04 lb/MMBtu 6 98.48 3.46E-04 lb/MMBtu 6 64.39 162.86
Lead&compounds H 1.54E-05 lb/MMBtu 6 4.38 1.54E-05 lb/MMBtu 6 2.87 7.25
Manganese&compounds TH 2.49E-03 lb/MMBtu 6 708.69 2.49E-03 lb/MMBtu 6 463.37 1172.06
Mercury,vapor Include in Merc &Com ds TH 1.15E-06 lb/MMBtu 6 0.33 1.15E-06 lb/MMBtu 6 0.21 0.54
Methanol H) 9.49E-06 lb/sf 2 740.22 4.13E-05 Ib/sf 2 2106.30 2846.52
Methyl bromide(H)(bromomethane) 3.53E-07 lb/sf 2,7 27.51 6.59E-07 Ib/sf 2,7 33.60 61.11
Methyl chloride H chloromethane) 2.66E-05 lb/MMBtu 6 7.57 2.66E-05 lb/MMBtu 6 4.95 12.52
Methyl chloroform TH (1,1,1 trichloroethane) 3.93E-05 lb/MMBtu 6 11.19 3.93E-05 lb/MMBtu 6 7.31 18.50
Meth 1 edi 1 ketone(TH) 1.01E-06 lb/sf 2,7 78.59 5.39E-06 lb/MMBtu 6 1.00 79.59
Methyl isobutyl ketone TH 9.63E-07 lb/sf 2,7 75.08 4.45E-04 lb/MMBtu 6 82.81 157.89
Methylene chloride(TH)(dichloromethane) 3.16E-07 lb/sf 2,7 24.61 5.91E-07 Ib/sf 2,7 30.13 54.74
Nap hthalene H 8.13E-06 lb/MMBtu 6 2.31 8.13E-06 lb/MMBtu 6 1.51 3.83
Nickel metal(Component of Nickel&Compounds)(TH) 1.17E-05 lb/MMBtu 6 3.33 1.17E-05 lb/MMBtu 6 2.18 5.51
itrQ henol,4- H 9.41E-08 lb/MMBtu 6 0.03 9.41E-08 lb/MMBtu 6 0.02 0.044
Pentabhloro henol TH 4.48E-08 lb/MMBtu 1 6 0.01 4.48E-08 lb/MMBtu 6 0.01 0.021

Boise Cascade-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) ^�/ r V
Emission Point(s): EP-09a-d,EP-10a-d l� �fV 114-�
2014 Actual Process Throughput: 7,666 Boiler operating hours/yr lI
42,098 ton wood/yr
470,707 MMBtu/yr Total Fuel Combusted
272,004 MMBtu/yr Green Wood Combusted
198,703 MMBtu/yr Dry Wood Combusted
78,000,000 sf/yr Hardwood Veneer Production
51,000,000 sf/yr Softwood Veneer Production
129,000,000 sf/yr Total Veneer Production
284,614 MMBtu/yr Btu of Wood Combusted-ratioed for Hardwood Veneer
186,094 MMBtu/yr Btu of Wood Combusted-ratioed for Softwood Veneer
Actual Emissions Summary:
Hardwood Softwood Total
Compound EmissionEmissions* Emissions* Emissions*
Factor Units Ref. Ib/ r Emission Factor Units Ref. Ib/ r Ib/ r
Perchloroeth lene PERC tetrachloroeth lene TH 2.46E-05 lb/MMBtu 6 7.00 2.46E-05 lb/MMBtu 6 4.58 11.58
Phenol(TH) 1.63E-06 lb/sf 2,7 127.34 3.41E-06 lb/sf 2 173.91 301.25
Phosphorus Metal,Yellow or White H 5.45E-03 lb/MMBtu 6 1551.14 5.45E-03 lb/MMBtu 6 1014.21 2565.35
Polychlorinated bi hen is TH 8.15E-09 lb/MMBtu 5 0.00 8.15E-09 lb/MMBtu 5 0.00 0.004
Pol c clic Organic Matter H 2.23E-05 lb/MMBtu 6 6.35 2.23E-05 lb/MMBtu 2 4.15 10.50
Pro ionaldeh de(H) 9.08E-07 ib/sf 2,7 70.79 2.14E-05 lb/MMBtu 6 3.98 74.77
Propylene dichloride H)(1,2 dichloro ro ane) 1.68E-05 lb/MMBtu 6 4.78 1.68E-05 Ib/MMBtu 6 3.13 7.91
Selenium compounds H 5.39E-07 lb/MMBtu 6 0.15 5.39E-07 lb/MMBtu 6 0.10 0.25
Styrene(TH) 3.87E-07 lb/sf 2,7 30.19 1.54E-05 lb/MMBtu 6 2.87 33.05
Tetrachlorodibenzo- -dioxin,2,3,7,8- (TH) 8.60E-12 lb/MMBtu 5 0.00 8.60E-12 lb/MMBtu 5 0.00 4.05E-06
Toluene(TH) 3.42E-07 lb/sf 2,7 26.70 3.67E-06 lb/MMBtu 6 0.68 27.38
Trichlorobenzene,1,2,4- H 6.75E-07 lb/sf 2,7 52.65 1.26E-06 lb/sf 2,7 64.32 116.97
Trichloroeth lene TH 1.99E-05 lb/MMBtu 6 5.66 1.99E-05 lb/MMBtu 6 3.70 9.37
Trichlorofluoromethane CFC 111 T 1.59E-05 lb/MMBtu 6 4.53 1.59E-05 lb/MMBtu 6 2.96 7.48
Trichloro henol,2,4,6- H 2.76E-07 lb/MMBtu 6 0.08 2.76E-07 lb/MMBtu 6 0.05 0.130
Vinyl chloride chloroethene TH 2.32E-07 lb/sf 2,7 18.12 4.34E-07 lb/sf 2,7 22.15 40.26
Vinylidene chloride 1,1-dichloroethene) TH 3.60E-07 lb/sf 2,7 28.10 6.33E-07 ib/sf 2,7 32.30 60.40
X lene(TH) 3.95E-07 lb/sf 2,7 30.77 1.87E-06 lb/sf 2 95.37 126.14
*Note: All emissions/include emissions from wood combustion and wood drying.
References: V
1-Stack Testing Data,1996
2-NCASI Wood Products Database,Updated 2013,Direct Fired Veneer Dryer
3-Based on Feb. 12,2010 stack test. PM 10 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-AP-42 Section 1.6,September 2006
6-Tables 4.1,4.3,4.5,5.1 of NCASI TB 1013,March 2013,median values(metal factors with mechanical collector,for multiclone).
7-Half the average detection values are used for non-detects.

R �Dc
f�CS'
P
Boise Cascade-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
j I
- 2014 Actual Process Throughput:
Natural Gas 15,166 therms/yr
1.49 MMcf/yr t
r--
Multiclone /
Natural Gas Control
Pollutant Emission Factor(1) Eff. (2) lb/yr tons/yr
CO 84 lb/MMcf -- 0.062✓
_ NOx 100 lb/MMcf -- 0.074✓
PM 7.6lb/MMcf 90% -- 0.0006
PM-10 7.61b/MMcf 90% -- 0.0006
PM-2.5 7.61b/MMcf 90% -- 0.0006
SO2 0.6lb/MMcf -- 0.0004
VOC 5.5 lb/MMcf -- 0.004
Arsenic 2.00E-04lb/MMcf 90% 2.97E-05 --
Benzene 2.10E-03 lb/MMcf 3.12E-03 --
Benzo(a)pyrene 1.20E-06 lb/MMcf 1.78E-06 --
Beryllium 1.20E-051b/MMcf 90% 1.78E-06 --
Cadmium 1.10E-03lb/MMcf 90% 1.64E-04 --
1
Chromium 1.40E-031b/MMcf 90% 2.08E-04 --
Cobalt 8.40E-05lb/MMcf 90% 1.25E-05 --
Formaldehyde 7.50E-02 lb/MMcf 1.12E-01 --
{ Hexane 1.80E+00 lb/MMcf 2.68E+00 --
Lead 5.00E-04lb/MMcf 90% 7.43E-05 --
Manganese 3.80E-04lb/MMcf 90% 5.65E-05 --
Mercury,vapor 2.60E-04 lb/MMcf 3.87E-04 --
Naphthalene 6.10E-04 lb/MMcf 9.07E-04 --
Nickel 2.10E-03lb/MMcf 90% 3.12E-04 --
POM 8.82E-05 lb/MMcf 1.31E-04 --
Selenium 2.40E-05lb/MMcf 90% 3.57E-06 --
Toluene 3.40E-03 lb/MMcf 5.06E-03 --
Notes-
1. AP42,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.
bs4\2015\Moncure Plywood\AEI\2014 AEI Contents\Moncure 2014 AEI Calcs vITBB NG 6/23/2015

i �
Boise Cascade-Moncure Plywood
Emission Source: Dry Waste System-Dry Waste Storage Silo
Source ID Number: ES-12,CD-21
Emission Point: EP-06,EP-12
2014 Actual Process Throughput:
Plywood Production 118,019,000 sf/yr
S
Emissions Summary:
Compound Emission Factor Reference Emissions
PM 9.29E-06 lb/sf 1 0.55 tpy
PM10 9.29E-06 lb/sf 1 0.55 tpy
i PM2.5 9.29E-061b/sf 1 0.55 tpy
References:
1. Emission factor from original Title V Permit Application
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Boise Cascade-Moncure Plywood
Emission Source: Sander System
Source ID Number: ES-04, CD-05
Emission Point: EP-05
2014 Actual Process Throughput:
Sander Operation Production 117,090 sf/yr
Emissions Summary:
{N Compound Emission Factor Reference Emissions
PM 1.1 5E-05 lb/sf 1 0.00 tpy
M10 1.15E-051b/sf 1 0.00 tpy
M2.5 1.15E-051b/sf 1 0.00 tpy
VOC 1.51E-04 lb/sf 2,3 0.01 tpy
Acetaldehyde 1.77E-06lb/sf 2 0.21 lb/yr
Formaldehyde 1.22E-06lb/sf 2 0.14 lb/yr
Methanol 7.73E-06lb/sf 2 0.91 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.
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Boise Cascade-Moncure Plywood OC
Emission Source: Dry Waste Transfer System
Source ID Number: ES-03,CD-06
Emission Point: EP-06
2014 Actual Process Throughput:
Hardwood Plywood Production 82,786,000 sf/yr
Softwood Plywood Production 35,233,000 sf/yr
iu Emissions Summary:
Softwood Hardwood
Compound Emission Factor Ref. Emission Factor Ref. Emissions
PM 6.60E-04lb/sf 1 1.15E-05lb/sf 1 12.10 tpy
PM10 6.60E-04lb/sf 1 1.15E-05lb/sf 1 12.10 tpy
PM2.5 6.60E-04lb/sf 1 1.15E-05lb/sf 1 12.10 tpy
I II
References: /
1. Emission factor from original Title V Permit Application I/
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Boise Cascade-Moncure Plywood
Emission Source: Hog Fuel Storage Silo
Source ID Number: IES-GWS (ES-11)
Emission Point: EP-11
2014 Actual Process Throughput:
I
Hog Fuel 20,584 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.
13
AP-42 Section 13.2.4:
U
E(lb/ton) =k x 0.0032 x 5
(m)1.4
2
where:
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
1
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 0.00041 tpy Y
PM10 1.87E-05 lb/ton 0.00019 tpy T
v PM2.5 2.83E-06 lb/ton 0.00003 tpy D '
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Boise Cascade-Moncure Plywood
Emission Source: Green Chip Sizing,Rechip, Transfer
Source ID Number: ES-17,ES-18,ES-14
I r' Emission Point: EP-14
2014 Actual Process Throughput:
I
Tons Green Chips 29,341 ton/year
Emissions Summary:
i
Compound Emission Factor Reference Emissions
PM 5.30E-02 lb/DT 1 0.39 tpy
PM10 5.30E-02 lb/DT 1 0.39 tpy
7 i PM2.5 5.30E-02 lb/DT 1 0.39 tpy
- References:
1. Weyerhaeuser Test Data,Title V Bulletin#19
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" Boise Cascade-Moncure Plywood
Emission Source: Plywood Waste Hog
Source ID Number: ES-16
Emission Point: EP-16
2014 Actual Process Throughput:
Tons Dry Wood 12,777 ton/year
d
Emissions Summary:
u}� Compound Emission Factor Reference Emissions
4
PM 5.30E-02 lb/DT 1 0.34 tpy
n M10 5.30E-02 lb/DT 1 0.34 tpy
! PM2.5 5.30E-02 lb/DT 1 0.34 Ty
References:
! 1. Weyerhaeuser Test Data,Title V Bulletin#19
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l Boise Cascade-Moncure Plywood
Emission Source(s): Glue Operations and Pressing
Source ID Number(s): ES-13
Emission Point: EP-13
t
2014 Actual Process Throughput:
4
Hardwood Plywood Production 82,786000 sf/yr
r Softwood Plywood Production 35,233:000 sf/yr \0
4fl 1
60
Hardwood Softwood Total
Compound Emission Emissions Emission Emissions Emissions
Factor Units Ref. ton/ r Factor Units Ref. ton/ r ton/ r
I( PM 2.00E-04 lb/sf 1 8.28 ✓ 2.00E-04 lb/sf 1 3.52 11.80
PM10 2.00E-04 lb/sf 1 8.28 ✓ 2.00E-04 lb/sf 1 3.52 11.80
PM2.5 8.32E-05 lb/sf 1 3.44 \/I 8.32E-05 lb/sf 1 1.47 v 4.91
VOC 1.71E-04 lb/sf 2 7.08 ✓ 5.87E-04 lb/sf 2 10.34 17.42
Total
�1 Compound Emission Units Ref. Emissions Emission Units Ref. Emissions Emissions
Factor Factor
- lb/yr lb/yr lb/ r
Acetaldehyde - 1 3.61E-06 lb/sf 1 127.19 127.19
Formaldehyde 5.00E-06 lb/sf 2 413.93 v 5.00E-06 lb/sf 2 176.17 590.10
Methanol 1.11E-04 lb/sf 2 9189.25 1.11E-04 lb/sf 2 3,910.86 13,100.11
Methyl Ethyl Ketone - 1 8.12E-07 lb/sf 1 28.61 28.61
Methyl Isobutyl Ketone -- 1 8.17E-07 lb/sf 1 28.79 28.79
Phenol 1.59E-05 lb/sf I I 1 1316.30 yr 2.71E-06 lb/sf 1 95.48 1,411.78
References:
k 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.
VOC factor is VOC as Carbon,converted to propane,adding formaldehyde and half of methanol.
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.
E 2._Press Compliance Test on December 10,2014�_ _
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Boise Cascade-Moncure Plywood
Emission Source: 250 BP Diesel-Fired Water Pump#1
Source ID Number: DES-19
2014 Actual Process Throughput:
Hours of Operation 133 Hr/yr
No.2 Fuel Oil Usage 1,375 gal/yr
Heat Input(250 hp) 84.6 MMBtu/yr
Compound Emission Factor Units Reference Emissions
ton/yr
~q CO 9.50E-01 lb/MMBtu 1 0.040
Ox 4.41E+00 lb/MMBtu 1 0.187
PM 3.10E-01 lb/MMBtu 1 0.013
PM10 3.10E-01 lb/MMBtu 1 0.013
oo
PM2.5 3.10E-01 lb/MMBtu 1 0.013 11
SO2 2.90E-01 lb/MMBtu 1 1.23E-02
OC 3.50E-01 lb/MMBtu 1 1.48E-02
Compound Emission Factor Units Reference Emissions
lb/yr
Acetaldehyde(TH) 7.67E-04 lb/MMBtu 1 0.065
crolein TH 9.25E-05 lb/MMBtu 1 0.008
Benzene(TH) 9.33E-04 lb/MMBtu 1 0.079
Benzo(a)pyrene T) 1.88E-07 lb/MMBtu 1 0.00002
Formaldehyde(TH) 1.18E-03 lb/MMBtu 1 0.100
Naphthalene (H) 8.48E-05 lb/MMBtu 1 0.007
Toluene(TH) 4.09E-04 lb/MMBtu 1 0.035
k ylene(TH) 2.85E-04 lb/MMBtu 1 0.024
POM 1.68E-04 lb/MMBtu 1 0.014
J References:
1 -AP-42,Section 3.3,Table 3.3-1,October 1996
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Boise Cascade-Moncure Plywood
Emission Source: 250 HP Diesel-Fired Water Pump#2 Y OS
Source ID Number: :.ES-23
1L.J 2014 Actual Process Throughput:
�u.
1� Hours of Operation 16 Hr/yr
No.2 Fuel Oil Usage 165 gal/yr
Heat Input(250 hp) 10.2 MMBtu/yr
'- Compound Emission Factor Units Reference Emissions
ton/yr
~V CO 9.50E-01 lb/MMBtu 1 0.005
Ox 4.41E+00 lb/MMBtu 1 0.0224
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
S02 2.90E-01 lb/MMBtu 1 1.48E-03
-�� OC 3.50E-01 lb/MMBtu 1 1.78E-03
Compound Emission Factor Units Reference Emissions
lb/yr
Acetaldehyde(TH) 7.67E-04 lb/MMBtu 1 0.008
'4 Acrolein(TH) 9.25E-05 lb/MMBtu 1 0.001
Benzene(TH) 9.33E-04 lb/MMBtu 1 0.009
Benzo(a) yrene (T) 1.88E-07 lb/MMBtu 1 0.000002
Formaldehyde TH 1.18E-03 lb/MMBtu 1 0.012
Naphthalene (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
'}} t References:
l., 1 -AP-42,Section 3.3,Table 3.3-1,October 1996
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Boise Cascade- Moncure Plywood �S
Emission Source(s): Vat Operations
Source ID Number(s): ES-20
Emission Point: EP-20
2014 Actual Process Throughput:
r--
Total Vat Production 93,000,000 sf/yr
i -
Emissions
Compound Emission Factor Units Reference ton/yr
VOC-Hardwood 1.20E-05 lb/sf 1,2 0.30
VOC-Softwood 7.70E-05 lb/sf 1,2 1.69
Total VOC 1.98
Compound Emission Factor Units Reference Emissions
lb/yr
Acetaldehyde 4.67E-06 lb/sf 1 434.31
Methanol 7.34E-06 lb/sf 1 682.62
References:
1. NCASI Database for Wood Products Manufactuers,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.)
! 2. Hardwood and softwood vat production is ratioed based on log throughput(gum and poplar vs pine,
respectively).
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Boise Cascade-Moncure Plywood
Emission Source(s): End Sealer Spray Booth
,— Source ID Number(s): ES-21
Emission Point: EP-21
r"
2014 Actual Process Throughput:
r r. End Seal Material Usage 2,700 gal/yr
Estimated Overspray 30.0%
Spray Booth Filter Efficiency 97.5%
i
Compound Emission Factor Units Ref Emissions
ton/yr
PM 90% %wt 1 0.07
PM10 90% %wt 1 0.07
VOC 0.4% %wt 2 0.04
Compound Emission Factor Units Ref Emissions
lb/yr
Vinyl acetate 0.031% %wt 2,3 6.70
References:
1. Conservatively assume 90%solids in material.Assume 30%overspray into filter.
2. Compound speciation from MSDS,April 2010. Specific gravity is 0.96.
3. Compound speciation from WVCO letter,April 26,2012.
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Boise Cascade-Moncure Plywood
Emission Source: Tongue and Groove Saw n�?'
Source ID Number: ES-22, CD-06
Emission Point: EP-06
j2014 Actual Process Throughput:
Saw Operating Hours 104 hours
t' Saw Production 1,238,927 sf/yr
Calculations for this source is based on the following assumptions:
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.
j ''', Conservatively assume baghouse efficiency of 99.5%.
Volume of Annual T&G- T&G
r Compound Total Panels T&G/Panel Dust Generated Rate
(per year) (ft3/panel) (ton/yr) (ton/hr)
PM 38,716 0.0104 7.179 0.069
a
. � Emissions Summary
'G Baghouse Annual
Compound Efficiency Emissions
(%) (lb/yr) (ton/yr)
r PM 99.5 71.79 0.036
PM10 2 99.5 23.04 0.012
_4
e PM2.5 99.5 10.27 0.005
Compound Emission Factor Reference Emissions
VOC 7.55E-05lb/sf 3 0.05 tpy
i w Acetaldehyde 5.59E-07lb/sf 3 0.69lb/yr
Formaldehyde 3.89E-07 lb/sf 3 0.48 lb/yr
i Methanol 6.82E-06 lb/sf 3 8.45 1b/yr
i
I—J 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 B.1,Section 10.5,October 1986. PM10 is assumed to be 32.1%of PM from
sander cyclone and baghouse. PM2.5 is assumed to be 14.3%of PM from sander cyclone and baghouse.
y r 3. Emission factors for VOC and organics based on NCASI Database for Wood Products Manufactures,
" updated February 2013,Sander,softwood plywood,uncontrolled median factor. VOC calculated as
sum of VOC as C,formaldehyde,and 50%of methanol factors.
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Boise Cascade-Moncure Plywood d
Emission Source: Bark Hog
r.
Source ID Number: IS-IN-1
{ Emission Point: IS-IN-1
2014 Actual Process Throughput:
J
-- Fuel Hogged 20,584 ton/yr
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
j 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 r PM 0.024 lb/ton
j PM 10 0.011 lb/ton
PM2.5 0.0046 lb/ton
Green Emission Inside Annual Annual
Compound Material Factor Building Emissions Emissions
( y) Qb/ton) Control(%) (lb/yr) (TPY)
( PM 20,584 0.024 95% 24.70 0.01
PM10 20,584 0.011 95% 11.32 0.01
PM2.5 20,584 0.0046 95% 4.69 0.002
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Boise Cascade-Moncure Plywood
L Emission Source: Core Chipping
Source ID Number: IS-IN-2
Emission Point: IS-IN-2
2014 Actual Process Throughput:
Cores Chipped 241 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
j 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.
r
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
r ° (tpy) (lb/ton) Control(%) (lb/yr) (TPY)
PM 241 0.024 95% 0.29 0.0001
PM10 241 0.011 95% 0.13 0.0001
r
PM2.5 1 241 1 0.0046 1 95% 1 0.05 1 0.0000
1
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Boise Cascade-Moncure Plywood
Emission Source: Green Veneer Hogging Operations
Source ID Number: IS_IN-3
j Emission Point: IS IN-3
^ 2014 Actual Process Throughput:
ut:
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Green Veneer Hogged 29,100 ton/year
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.
PM 0.024 lb/ton
PM 10 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 29,100 0.024 95% 34.92 0.02
PM10 29,100 0.011 95% 16.01 0.01
'l PM2.5 29,100 0.0046 95% 6.63 0.003
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Boise Cascade-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
2014 Actual Process Throughput:
J �
Logo paint usage 890 gal/yr
Ink usage 385 gal/yr
y' Ink density 8.21 lb/gal
Emissions Summary:
i
Compound Emission Factor Reference Emissions
i VOC-logo paint I 4.00E-01 lb VOC/gal 1 1 0.18 tpy
VOC-ink I 2.00E-01 Ilb VOC/lb 1 1 1 0.32 tpy
Total VOC 0.49 tpy
References:
r 1. Material Safety Data Sheets
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7— Boise Cascade-Moncure Plywood w
Emission Source: Plywood Surface Patching
Source ID Number: IS-IN-6
Emission Point: IS-IN-6
2014 Actual Process Throughput:
Plywood Surface Patching(Part A) 15,050 gal/yr
Density 12.58 lb/gal
Plywood Surface Patching(Part B)' 2,316 gal/yr
Density 10.33 lb/gal
Plywood Surface Patching(W.B.Face) 4,950 gal/yr
I Emissions Summary:
Compound Reference Emissions
f r Component Units lb/ r tons/ r
i VOC-U-100-A Patch 0.02% %wt 2 37.9 0.02
VOC-W.B.Face 0.25 lb/gal 3 1,237.5 0.62
MDI-U-100-B Patch 38% %wt 1 negligible negligible
References: ��
r , �b
1. Material Safety Data Sheet for U-100-B Patch Catalyst,April 2014. Due to the extremely low vapor
i pressure of the material(<0.000001 mmHg)per the manufacturer's MSDS,VOC and HAP emissions
from the use of this product are assumed to be negligible.(The MSDS shows 0%VOC.)
2. Material Safety Data Sheet for U-100-A Patch,April 2014. _ VS
_ __
3.FMaterial Safety Data Sheet for Putty W.B.Face-Pine,January 1994.MSDS states there are no
reportable quantities of ingredients present and no chemicals subject to reporting requirements. W _
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Boise Cascade-Moncure Plywood
Emission Source: Maintenance Parts Washer
Source ID Number: IS-IN-7
Emission Point: IS-IN-7
2014 Actual Process Throughput:
Gallons Used 110 gal/yr
Emissions Summary:
Compound Emission Factor Reference Emissions
VOC I 7.00E+00 lb/gal 1 1 0.39 tpy
r ,
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References:
1. Material Safety Data Sheet
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Boise Cascade-Moncure Plywood
Emission Source: Veneer Diverter Exhaust Cyclone
—; Source ID Number: IS-IN-8
Emission Point: IS-IN-8
2014 Actual Process Throughput:
Green Veneer 162,377 ton/yr
Emissions Summary:
Compound Emission Factor Reference Emissions
PM I 5.30E-02 lb/DT 1 1 2.15 tpy
PM10 I 5.30E-02 lb/DT 1 1 2.15 tpy
1
References:
1. Weyerhaeuser Test Data,Title V Bulletin#19,max green chips factor
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Boise Cascade-Moncure Plywood
Emission Source: Green Veneer Stackers
Source ID Number: IS-IN-9,IS-IN-10
Emission Point: IS-IN-9,IS-IN-10
2014 Actual Process Throughput:
Green Veneer 162,377 ton/yr
r
Emissions Summary:
Compound Emission Factor Reference Stacker
Emissions
PM 1.40E-02 lb/DT I 1 1 0.57 tpy
PM10 I 1.40E-02 lb/DT I 1 0.57 tpy
References: /
l 1. Weyerhaeuser Test Data,Title V Bulletin#19,average green chips factor J
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Boise Cascade-Moncure Plywood
Emission Source: Hammer Hog Truck Dump
Source ID Number: IS-IN-11
Emission Point: IS-IN-11
'7 2014 Actual Process Throughput:
Dry waste 2,006 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. ( 13
AP-42 Section 13.2.4: E (lb/ton) =k x 0.0032 x ` 5
1
(m) .4
where:
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
I` 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)_
i PM factor= 3.96E-05 lb/ton
PMIo factor= 1.87E-05 lb/ton
PM2.5 factor= 2.83E-06 lb/ton
i
LJ Compound Emission Factor Emissions
PM 3.96E-05 lb/ton 0.000 tpy
PM10 1.87E-05 lb/ton 0.000 tpy
PM2.5 2.83E-06 lb/ton 0.0000 tpy
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Boise Cascade-Moncure Plywood
Emission Source: Dry Waste Truck Dump
r Source ID Number: IS-IN-12
Emission Point: IS-IN-12
2014 Actual Process Throughput:
Dry waste 944 ton/yr
r
Emissions Summary:
Emissions are calculated use the"drop loading equation"from AP-42 Section
13.2.4(Aggregate Handling and Storage Piles),November 2006. 1.3
U
AP-42 Section 13.2.4: E(lb/ton) =k x 0.0032 x 5 ml.4
where:
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
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 0.000 tpy
PM10 1.87E-05 lb/ton 0.0000 tpy
PM2.5 2.83E-06 lb/ton 0.0000 tpy

COPY of RECORD Date Submitted: 6/23/2015 15:27:21
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:
6/23/2015—Emission Source Comments
ES IES 19 :IES-23 is not listed on the List of Emission Sources,but is listed under this source. Please list individually.
6/2/2015—General Comments
General Comments: 1. Due to extremely low vapor pressure of material in OS-6,emissions are assumed to be negligible.2.
Some criteria pollutant emissions for OS-2,OS-3,OS-4,OS-6,OS-16,OS-24,OS-25,OS-34 and OS-35 are below the
AERO reporting threshold but can be viewed in the calculations. 3.ES15 has been removed from the permit. Please remove the
emission source from AERO.
79

1-7 Boise Cascade-Moncure Plywood
Annual Activity and Usage Information
2014 Air Emissions Inventory
Activity and Usage 2014 Annual Amount
Vat Production 93,000,000 ft2(3/8")
Hardwood Veneer Production 78,000,000 ft2(3/8")
r-
Softwood Veneer Production 51,000,000 ftZ(3/8")
Hardwood Plywood Production 82,786,000 ftZ(3/8")
Plywood 2
Production Softwood Plywood Production 35,233,000 ft (3/8")
Plywood Press Hours of Operation 7,180 hours
Sander Production 117,090 ft2(3/8")
T&G Saw Production 1,238,927 ft2(3/8")
T&G Saw Hours of Operation 104 hours
Pine Logs 97,974 tons
Log Throughput Gum Logs 93,395 tons
Poplar Logs 16,807 tons
Boiler Hours of Operation 7,666 hours
' Total Dry Wood Combustedl 12,777 ton(as fired)
Dry Wood Heat Content 7,776 Btu/lb
Total Dry Wood Combusted 198,703 MMBtu/yr
Green Chips.Purchased for Combustion 5,737 tons chips
Green Chips Combusted 3,000 tons chips
Green Chips Heat Content 2 4,541 Btu/lb
Total Green Chips Combusted 79,349 MMBtu
Total Hog Fuel Combusted' 20,584 ton(as fired)
Plant wide Fuel Poplar Bark Heat Content 5,703 Btu/lb
Combustion Gum Bark Heat Content2 4,952 Btu/lb
Pine Bark Heat Content2 4,018 Btu/lb
Total Hog Fuel Combusted 192,655 MMBtu
Total Green Fuel Combusted 272,004 MMBtu
Total of All Fuel Combusted 470,707 MMBtu
}
Boiler Efficiency 86.0% %
Natural Gas Combusted 15,166 therms
250 HP Diesel Fired Water Pump#1 1375 gal/yr
133 hr/yr
250 HP Diesel Fired Water Pump#2 165 gal/yr
16 hr/yr
Veneer Diverter 162,377 ton/yr
Miscellaneous Hammer Hog Truck Dump 2,006 ton/yr
Dry Waste Truck Dump 944 ton/yr
Core Chipping and Handling 241 ton/yr
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Boise Cascade-Moncure Plywood
Annual Activity and Usage Information
2014 Air Emissions Inventory
- Activity and Usage 2014 Annual Amount
Green Veneer Hogging Operations 29,100 ton/yr
Maintenance Parts Washer 110 gal/yr
End Seal Paint 2,700 gal/yr
Paint Usage(Logo painting) 890 gal/yr
Miscellaneous Ink Usage 385 gal/yr
Green Veneer Stackers 162,377 ton/yr
Plywood Surface Patching(W.B.Face) 4,950 gal/yr
Plywood Surface Patching(Part A) 15,050 gal/yr
Plywood Surface Patching(Part B) 2,316 gal/yr
Cores Sold in 2014 759,294 cores
Ash Total Wood Ash 263 tons
Total Wood Ash sent offsite 263 tons
PF Resin Usage PF Resin Application Rate 39 Tons/MMSF
PF Resin Usage 4,660 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.
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I '
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