AQ_F_1900039_20130626_EI_Cmb-EI-File

0
,CY2012 Emission Inventory Review/Data Tracking Form
�L
Check boxes that apply.
Facility Name: OK CKVe I ��rd� Facility ID: /q d0® 3 q
Assigned To: Confidential Request: Yes ❑ No
1 'P(AMVA If yes, notify El coordinator and treat as confidential.
Su ssion type: AERO Paper❑ If Paper, initials of person entering emissions data into ED
Inventory Review/IBEAM Data Entry
Y N*
All forms appear complete and signed by the appropriate official.
Supporting calculations,control efficiencies,and documentation of emission factors,if not using
AP-42,are included and appear correct.
Pertinent compliance and permitting limits checked and.facility is at or below limits(If facility has
exceeded limit, check calculation and explain).
All permitted and known insignificant sources are included and source and control device IN are
the same as the Ids used in the Air Permit.
All known operating scenarios,control devices,and emission release points have been entered for
each source.
For any pollutant,all emissions have been reported for all permitted and insignificant sources that
contribute to the facility total (above de minimus reporting limits)of that pollutant to the best of IJ
reviewers knowledge.
All volatile HAPS/TAPS included in VOC total. (See pollutant list on DAQ external web page)
r
Significant changes(>105/o)from previous inventories have been investigated and found acceptable
(verified by running QAQC report and Facility Total report in ED-Entry). Print Facility total report and
attach.
Reviewer has checked for facility comments and addressed any issues in the facility comments.
Reviewer has checked for SCC/source type accuracy and corrected errors when found. (please
note errors corrected in summary below).
Summary of all changes/additions to inventory:
C��'e��► WOOd �4 of 5-t-;%X5? s;II o (05-1� ) were kePdVfe
, eider C--,s it wh se_h -i� no j6ng-er vu peiw3rt 'J& ?tki I-A4 z O_#
WA-5 t orrepte d -to 1 e3-CTwS to be uks`steut with 1- Pew` l�
-7tu,ff wcKea5e TN VOcIPMP / TaiP)/PP5,- due to -fie pltivaod
bus wert — 7. 1- fro, fk rzvlw-� eft• ;[T lased d` reAt C-T-
I No, explain corrects a ac Ion to en In the summa section o his for
QAQC and Facility Total Reports verified correct? ❑
Has the Data Entry Complete da been entered in IBEAM? ❑ (do so only when totally finished)
Signature of Reviewer: Date reviewed:!
(This signature certifies that this ew was completed to the best of my ability within the time constraints allowed.)

Facility Total CY 2012 Emission Summary Recorded in ED Facility ID #: 1900039
Facility Name: Moncure Plvwood Permit#(s): 03424T22
Green House Gases Pollutants(GHG) Actual Emissions
Tons/Yr
Pollutant CAS
Demini- Change
mus
Not Not N/A
Reported Reported
CO2 equivalent(sum of individual GHG pollutant emission No GHGs
times their 1995 IPCC Global Warming Potential (GWP), Reported
converted to metric tons)
Criteria Pollutants Actual Emissions
(Tons/Year)
Pollutant CAS CY 2012 CY 2011 Demini- %
from ED from Fees mus Change
CO CO 27.29 25.78 0.5 5.9%
NOx NOx 38.94 41.08 0.5 -5.2%
PM(TSP) TSP 57.64 49.68 0.5 16.0%
PM10 PM10 57.64 49.01 0.5 1,17.6%
PM2.5 PM2.5 52.93 46.90 0.5 12.9%,
S02 S02 3.55 3.74 0.5 -5.1%
VOC VOC 51.77 43.05 0.5 20.37
Hazardous Air Pollutants(HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPs) (Pounds/Year)
Pollutant CAS CY 2012 CY 2011 Demini- %
from ED from Fees mus Change
Antimony & Compounds (total mass, inc elemental SB) Z24 2.36 10.0 I -5.1%
Antimony Unlisted Compounds-Speck Compound SBC-Other 2.24 2.36 10.0 -4.9%
(Component of SBC)
Arsenic & Compounds(total mass of elemental AS, arsine and 0.210160 1 0.221010 0.01 -4.9%
all inorganic compounds)
Arsenic Unlisted Compounds-Specify-Compound ASC-Other 0.210160 0.221010 0.01 -4.9%
(Component of ASC)
Beryllium & compounds (Total mass) 0.312390 0.328530 1.0 -4.9%
Beryllium Metal (unreacted) (Component of BEC) 7440-41-7 0.312390 0.328530 1.0 -4.9%
Cadmium & compounds (total mass includes elemental metal) 7.52 9.53 0.1 -21.1
10/14/2013 Page 1 of 4

Facility Total CY 2012 Emission Summary Recorded in ED Facility ID#: 1900039
Facility Name: Moncure Plywood Permit#(s): 03424T22
Hazardous Air Pollutants(HAPs) Actual Emissions
and/or Toxic Air Pollutants(TAPs) (Pounds/Year)
Pollutant CAS CY 2012 CY 2011 Demini- %
from ED from Fees mus Change
Cadmium Metal, elemental, unreacted(Component 7440-43-9 7.52 9.53 0.1 -21.2%
of CDC)
Chromium-A1UTotal(includes Chromium (VI) categories, 5.96 6.01 0.1 -0.8%
metal and others)
Chromic acid(VI) (Component of SolCR6& CRC) 7738-94-5 0.993980 0.788160 0.01 126.1%
Chromium Unlisted Compounds-Specify CRC-other 4.97 5.23 0.1 -4.9%
Compound(Component of CRC)
Chromium (VI)Soluble Chromate Compounds(Component of 0,993980 0.788160 0.01 126.1%
CRC)
Chromic acid(VI) (Component of SolCR6& CRC) 7738-94-5 0.993980 0.788160 0.01 12-6.1%
Cobalt& compounds 1.85 1.94 1.0 -4.6%
Cobalt Unlisted Compounds-Specify Compound COC-Other 1.85 1.94 1.0 -4.9%
(Component of COC)
Lead& compounds 13.63 14.34 1.0 -5.0%
Lead Unlisted Compounds-Speck Compound PBC-Other 13.63 14.34 10.0 -4.9%
(Component of PBC)
Manganese & compounds 454.39 477.86 10.0 I -4.9%
Manganese Unlisted Compounds-Specify MNC-Other 454.39 477.86 10.0 -4.9%
Compound(Component of MNC)
Mercury & Compounds-all total mass includes Hg Vapor 0.993980 1.05 0.001 I -5.3%
Mercury, vapor (Component of HGC) 7439-97-6 0.993980 1.05 0.001 -4.9%
Nickel& Compounds,sum total mass includes elemental 9.37 9.86 1.0 -5.0%
Nickel metal (Component of NIC) 7440-02-0 9.37 9.86 1.0 -4.9%
Polycyclic Organic Matter(7 PAH Compounds for NIF) 0.738400 0.776530 1.0 I -4.9%
Benzo(a)pyrene (Component of 833291POMTV& 50-32-8 0.738400 0.776530 1.0 -4.9%
5655317PAH)
Polycyclic Organic Matter(Specific Compounds from OAQPS 28.29 29.75 1.0 I -4.9
or.TP)
10/14/2013 Page 2 of 4

Facility Total CY 2012 Emission Summary Recorded in ED Facility ID #: 1900039
Facility Name: Moncure Plvwood Permit#(s): 03424T22
Hazardous Air Pollutants(HAPs) Actual Emissions
and/or Toxic Air Pollutants(TAPS) (Pounds/Year)
Pollutant CAS CY 2012 CY 2011 Demini- %
from ED from Fees mus Change
Benzo(a)pyrene (Component of 833291POMTV& 50-32-8 0.738400 0.776530 1.0 -4.9%
56553/7PAH)
Naphthalene (Component of 83329/POMTV) 91-20-3 27.55 28.97 1.0 -4.9%
Acetaldehyde 75-07-0 5,051.54 3,652.78 10.0 138.3%
Acrolein 107-02-8 371.04 282.78 10.0 131.2%
Benzene 71-43-2 216.53 168.95 1.0 28.2%
Carbon tetrachloride 56-23-5 12.78 13.44 1.0 -4.9%
CFC-11 (Trichlorofluoromethane)' 75-69-4 11.64 12.25 100.0 -4.9%
Chlorine 7782-50-5 224.36 235.94 100.0 . -4.9%
Chlorobenzene 108-90-7 9.37 9.86 10.0 -4.9%
Chloroform 67-66-3 7.95 8.36 100.0 -4.9%
Cumene 98-82-8 2,09T.91 2,274.51 100.0 -7.8%
DEHP (Di(2-ethylhexyl)phthalate) 117-81-7 - 0.013350 0.014030 10.0 -4.8%
Dinitrophenol, 2,4- 51-28-5 0.051120 0.053750 0.1 -4.9%
Ethyl benzene 100-41-4 8.80 9.26 100.0 -4.9%
Ethyl chloride (chloroethane) 75-00-3 55.39 59.85 10.0 -7.5%
Ethylene dichloride (1,2-dichloroethane) 107-06-2 86.02 92.76 1.0 -7.3%
Formaldehyde 50-00-0 2,280.33 2,100.20 10.0 8.6%
Hydrogen chloride (hydrochloric acid) 7647-01-0 159.04 5,674.56 100.0 1-97.2. %
MEK(methyl ethyl ketone, 2-butanone) 78-93-3 318.78 307.90 100.0 3.5%
Methanol (methyl alcohol) 67-56-1 11,960.94 9,786.39 1,000.0 122.2%
Methyl bromide (bromomethane) 74-83-9 83.70 91.29 1.0 -8.3%
Methyl chloride (chloromethane) 74-87-3 6.53 6.87 1.0 -4.9%
Methyl chloroform 71-55-6 8.80 9.26 100.0 -4.9%
Methylene chloride 75-09-2 74.73 81.11 1.0 -7.9%
MIBK (methyl isobutyl ketone) 108-10-1 645.57 766.65 10.0 1-15.8%
Nitrophenol, 4- 100-02-7 0.031240 1 0.032850 10.0 1 -4.9%
10/14/2013 Page 3 of 4

Facility Total CY 2012 Emission Summary Recorded in ED Facility.ID#: 1900039
Facility Name: Moncure Plywood Permit#(s): 03424T22
Hazardous Air Pollutants(HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPs) (Pounds/Year)
Pollutant CAS CY 2012 CY 2011 Demini- %
from ED from Fees mus Change
Pentachlorophenol 87-86-5 0.014480 0.015230 1.0 -4.9%
Perchloroethylene (tetrachloroethylene) 127-18-4 10.79 11.35 100.0 -4.9%
Phenol. 108-95-2 1,476.73 1,599.60 100.0 -7.7%
Phosphorus Metal, Yellow or White 7723-14-0 7.67 8.06 1.0 -4.9%
Polycyclic Organic Matter(Inc PAH, dioxins, etc.NCPOM 35.50 , 37.34 1.0 -4.9%
&AP 42 historic)
Propionaldehyde 123-38-6 232.93 242.15 10.0 -3.8%
Propylene dichloride (1,2-dichloropropane) 78-87-5 9.37 • 9.86 10.0 -4.9%
Selenium Compounds SEC 0.795190 0.836250 10.0 -4.9%
Styrene 100-42-5 152.06 136.96 100.0 11.0%
TCE(trichloroethylene) 79-01-6 8.52 8.96 1,000.0 -4.9%
Toluene 108-88-3 320.83 239.68 100.0 133.9%
Trichlorobenzene, 1,2,4- 120-82-1 160.28 173.58 100.0 -7.7%
Trichlorophenol,2,4,6- 88-06-2 0.006250 0.006570 1.0 -4.9%
Vinyl acetate 108-05-4 8.19 8.71 100.0 -6.0%
Vinyl chloride 75-01-4 54.69 59.41 0.1 -7.9%
Xylene (mixed isomers) 1330-20-7 338.85 295.98 100.0 14.5%
Largest Individual HAP Methanol (methyl alcohol) 11,960.94 lbs
Total HAP Emissions 6,703.44 lbs
DAO's Comments Regarding Inventory
10/14/2013 Page 4 of 4

306 Corimh Rd
Weyerhaeuser P.O.Box 230
Moncure,NC 27559559
The future is growing" (919)-542-2311
FAX[phone]
Certified Mail
7000 0600 0021 7089 8480
February 14, 2003
Donald R. van der Vaart, Ph. D., PE
NCDENR—Air Permits Section
Major Source Permits Branch
1617 Mail Service Center
Raleigh, NC 27699-1617
RE: Weyerhaeuser Company—Moncure Plywood
Title V Permit: 03424T.15 Facility ID 05119100039
Reference Request for Toxic Air Pollutants
Modeling Study for the Moncure Area
Per your letter dated January 16, 2002, the Moncure Plywood facility submits emission rates for
Formaldehyde, Hydrogen Chloride, Hydrogen Fluoride and Lead for our Facility for future modeling
efforts to be conducted by NCDENR.
In addition, enclosed you will find: a) a Plot Plan for the Moncure facility with the UTM coordinates,
b) Excel spreadsheets that contains specific UTM coordinates of the property lines and for the main
Plywood building, and c) Stack parameters.
If you have any questions or need any additional information,please contact me at(919) 542-231 1.
Sincerely,
Mike Swanson
Environmental Supervisor, Moncure
Enclosure: Plot Plan
UTM Coordinate
Stack Parameters
Emissions Spreadsheet
Cc: Perry Anglin— Weyerhaeuser - Moncure
Walter Wagner- Weyerhaeuser - Moncure
Chuck Vaught— Weyerhaeuser- New Bern

Weyerhaeuser
Moncure Plywood
Source Specific Emissions Summary Table
Maximum Allowable Emissions Summary Table
INPUT PARAMETERS:
Total Pine Production - sf
Total Hardwood Production 170.000,000 sf
PINE HARDWOOD Total Emissions
Permit Grou Sources) Pollutant Process Rate Emission Factor Units Emissions Process Rate Emission Factor Units Emissions Units
ES01 FBB and 2 Dryers Formaldehyde' 0 2.516E-05 Ib/sf 01 170000000 9.833E-06 Ib/sf 0.00010 Ib/hr
ES09&10 Direct heated Hydrogen Chloride= 0 lb/ton 0 80 5.60E-04 Ib/tnmBtu 0.0448 Ib/hr
CD-02 Multicyclone Hydrogen Flouride N/A
Lead ol lb/ton 0.0001 4.761:-OS Ib/mmBtu 0.004 Ib/hr
0.306 lb/month
ES-12 Drywaste System- Formaldehyde' N/A
Hydrogen Chloride= N/A
H dro en Flouride N/A
CD-21 Dry Waste Storage Silo Lead'
N/A
ES-04 Sander System Formaldehyde' N/A
H dro en Chloride 2 Hydrogen Flouride N/AN/A
Lead
N/A
ES-03 Dry Waste Transfer System Formaldehyde N/A
CD-06 Hydrogen Chloride 2 N/A
H dro en Flouride N/A
Lead'
N/A
ES-I I Hog Fuel Storage Silos Formaldehyde' N/A
Hydrogen Chloride'
N/A
Hydrogen Flouride N/A
LEdro
d'
N/A
ES-17 yde'
N/A
Chloride Z N/A
US-I8 Rechipper System Flouride N/A
ES-14
N/A
ES-I3 Glue Operations and Pressing Formaldehyde' 01 5.815E-06 Ib/sf 01 170000000 1.221 E-06 Ib/sf 0.00001 Ib/hr
Hydrogen Chloride N/A
Hydrogen Flouride N/A
Lead'
N/A
The Formaldehyde hourly rate was calculated by dividing by the maximum.8760 hours
Hydrogen Chloride is based using an emission factor of 5.6E-04. Based on emission tests conducted on several Weyerhaeuser's Boilers. Information is found in NCASI database
Lead is based using 4.76E-05 from APA2 Table 1.6-0/A
02/14/2003
Moncure Plywood

Y�
``. MonCUre Plywood Plant
Moncure Plywood LLC
306 Corinth Rd
P.O.Box 230
Moncure,NC 27559
(919)-542-2311
FAX[phone]
Certified Mail/Return Receipt Request
70121010 0003 3594 5654
June 25, 2013
Patrick Butler
TIN; ? 6 9013
Raleigh Regional Office
1628 Mail Service Center
Raleigh,NC 27699-1628
Per General Conditions 3.X of Title V Permit 03424T22,Moncure Plywood LLC submits our annual
Air Emissions Inventory for 2012.
If you have any questions or need additional information,please contact Brian Van Gelder, Project
Manager, at(803) 581-9261 or cell at(803) 374-3564.
S' erely
Y
Brian Van Gelder
Project&Environmental Manager
Enclosures: (2)2012 North Carolina Air Emissions Inventories
Cc: Brian Van Gelder—Moncure Plywood LLC

TABLE 1. EMISSION FACTOR (EF) COMPARISON
POLLUTANT "OLD" EF "NEW" EF CHANGE IN EF
2) (LB/FT2)
(LB/FT (LB/1000 FTz)
HARDWOOD
Formaldehyde 9.14 E-05 9.83 E-06 -0.0816
VOC 6.51 E-04 2.41 E-04 -0.410
PM 1.17 E-03 1.64 E-03 +0.470
NOx 2.70 E-04 5.45 E-04 +0.275
CO 3.92 E-05 3.76 E-04 +0.337
PINE
Formaldehyde 1.14 E-03 2.52 E-05 -1.11
VOC 3.75 E-03 1.07 E-03 -2.68
PM 9.55 E-04 1.21 E-03 +0.255
NOx 5.29 E-04 5.45 E-04 +0.016
CO 4.69 E-04 6.10 E-04 +0.141
NOTE: The "old" emission factors were calculated based on testing performed in 1994/1995.
The "new" emission factors were calculated based on testing performed in April 1996 at the
Moncure facility. Also note that NOx was not retested in 1996; however, per NCDEHNR
guidance, the "old" NOx emission factors were revised to reflect worst-case NOx emissions.
As discussed in the permit modification application submitted in October 1995, Willamette had
previously taken a production limit of 134MM ft2 to avoid Prevention of Significant
Deterioration (PSD) permitting. The emissions which corresponded to this production rate were
based on AP-42 emission factors. The extensive testing that Willamette has completed at the
Moncure facility has shown that all criteria pollutant emission levels are below the 250 tons per
year PSD threshold at a production rate of 170MM ft' per year.
3

DIVISION OF AIR QUALITY
May 26,2010
MEMORANDUM
To: Patrick Butler,Raleigh Regional Office
From: Betty Gatano, Stationary Source Compliance Branch(SSCB)
Subject: Moncure Plywood,LLC
Moncure, Chatham County,North Carolina
Air Permit No. 03424T21 Facility ID 05/19/00039
Particulate Emission Testing Performed February 12,2010 on Veneer Dryer M72(Source ES 10)
By Environmental Source Samplers, Inc.
Tracking No. 2010-022ST
The subject test report has been reviewed. The emission sources are fluidized bed wood burner ID No.
ESO1-A with blending chamber and dedicated overfire air fans, direct wood-fired veneer dryer M62 (ID
No. ES09)and direct wood-fired veneer dryer M72 (ID No. ES10). Burner ESO1-A supplies direct heat to
the two veneer dryers. The permitted maximum heat input rate to the burner is 80.0 million Btu per hour.
Particulate matter(PM)emissions from the wood burner are controlled with a multicyclone(ID No.
CD02), and PM emissions from the veneer dryers are uncontrolled. Testing was conducted only on veneer
dryer M72, which is representative of worst case(on mass emission rate in pounds per hour basis)total PM
emissions. The test demonstrates that the sources were operating in compliance with the PM emissions
standards during the testing period.
15A NCAC 2D .0515 Particulates From Miscellaneous Industrial Processes applies to the entire process,
from the wood burner to the two veneer dryers and limits the total PM from all emission points in the
process. The entire process has eleven emission points. The multicyclone outlet on the wood burner has
one emission point, and each dryer has five emissions points. As a worst case estimate of emissions,the
PM emission rate from the entire process is calculated as twice the total mass emission rate from the five
M72 emission points. The test results are given in the table below.
Test Results(lb/hi)
Pollutant e . Standard. Emission _. _ Compliance°
Limit(1bli) M72 a,M72 �' M72 �" M72° ` M72 " ' Total for all` `Process 'Indicated
Stack 1 Stackr2 Stack 3 Stack 4' Stack 5 M72 Stacks Total
Filterable PM 0.418 0.418 0.385 1.380 0.606 N/A
3.208 6.416
Condensible 15A NCAC 24.610* 0.101 0.019 0.031 0.248 0.560 N/A
PM 2D.0515 0.959 1.919
Total PM 0.520 6.437 0.416 1.628 1.167 Yes
4.167 8.334
*The allowable emission rate for PM is calculated as E=4.10(P)°67 for process rates less than or equal to 30 tons per hour(tph)and as E_
55.0(P)°"-40 for process rates greater than 30 tph.
Emissions testing was conducted at an average production rate of 13,558 square feet per hour(ft2/hr)on
veneer dryer M72, which is 91% of the maximum normal operating process rate of 14,859 feller. Veneer
dryer M62 operated at an average production rate of 8,528-fz/hr during testing. The production rate from
both dryers was 22,086 ftz/hr or 14.51 tons per hour during test.l
t The facility provided a conversion factor of 0.657 tons/thousand ftZ.

Patrick Butler,Raleigh Regional Office Chatham County
May 26,2010
Page 2(Moncure Plywood,LLC,PM Emissions,February 12,2010 Test)
Under Condition 2.LA.5 under Air Permit No. 03424T2,the facility was required to monitor the static
pressure drop and excursion values across the multicyclone ID No. CD02 used to control emissions from the
fluidized bed wood burner ID No. ESO1. The facility reported a range of static pressure drop during
testing of 2 to 3 inches of water. No excursions occurred during testing.
In conclusion,the results of the emission test conducted on Veneer Dryer M72(Source ES 10)are accepted
and demonstrate compliance with the PM standards for the subject emission sources. If you have any
questions,please contact me at(919)733-1478.
cc: Central Files, Chatham County
IBEAM Documents— 1900039

2012 NORTH CAROLINA
AIR EMISSIONS INVENTORY
Prepared for:
Moncure Plywood, LLC.
306 Corinth Road
Moncure, North Carolina 27559
Prepared by:
UM
URS Corporation — North Carolina
1600 Perimeter Park Drive I Suite 400
Morrisville, North Carolina 27560
[phone]
URS Project No. 31828920
June 2013

L � ..
'TABLEOF CONTENTS
Inventory Certification_Letter A
Emission Source & Operating Scenario List B
List of Emission Sources & Control Devices. C
(� Facility Summary
Emission Source Operating Scenario Forms E
Supporting Data F
� i
d.
r�
1-
L
y
1 �
P:IIOBS420IMMONCURE PLYWOOD-013 AEATOC.DOCX

Inventory Certification Form(Title V)
Facility Name: Moncure Plywood,LLC Facility ID : 1900039
306 Corinth Road Permit: 03424
Moncure,NC 27559 County: Chatham
DAQ Region : Raleigh
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2012
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:
(Important: Legally Resl2omible Official. read and sign after all sublai.5sionse finau
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
penalties 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 Si ned:
Printed Name: Jeffrey Matuszak
-Signature: XL
This form pl` rtle V facilities. If s 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: A ri Gi+ us -, (?- ri
Information on this Form cannot be held confidential
133

As entered in AERO
Facility Name: Moncure Plywood,LLC 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 *CS Description * CD ID's
Air Permit
ES—1 1 Green wood fuel storage silo
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 1D No.
ES-01—A)(NSPS Subpart Dc)
ES03—CC Core composer with saw
ES03—CS Core saw (green or dry veneer)
ES03—PSS Panel sawing system
ES03—SMS-1 String machine including saws CS-3 bagfilter(7,095 square feet of filter CD03—WWTC,CD06
area), dry waste transfer cyclone
ES03—SMS-2 String machine including saws
ES03—SS Strip saw
Bagfilter(6,200 square feet of filter
ES04 Wood sander CS-10 area),Woodwaste transfer cyclone(154 CD05,CD03—WWTC,
inches in diameter),Bagfilter(7,095 CD06
square feet of filter area),
ES09 M62 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
1

Cyclone(60 inches in
f 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
bagfilter(7,095 square feet of filter
Plywood waste hog g
ES 16 P1 CS-3 CD.03—WWTC, CD06
. area), dry waste.transfer cyclone
Cyclone(60 inches in
Green wood sizing operations diameter),Woodwaste transfer cyclone CD1.8,CD03—WWTC,
ES17 including sizing screens and CS-12
(154 inches in diaineter),Bagfilter CD06
bins (7,095.sq4are feet of filter area);
ES20 Vat.operations
ES21 End.sealer spray booth
Tongue and:groove saw bagfilter(7,095 square feet of filter
ES22 CS-7 CD06
(plywood.finishing) area).
I-1 Bark_ hogging operations with -
two saws
-j
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 Bogging . . .
I-4 Logo.painting and ink marking
I-5. Logo painting and ink marking
I-6 _. Plywood surface patching
I-7. Maintenance parts washers .
I=8 Veneer diverter exhaust
cyclone
green wood veneer stacker No.
I-9
n. 1:
Diesel—fired.water pump(250
IES 19 Horsepower maximum power
output)for emergency,purposes
i only
LJ
�I
2

As entered in AERO
Facility Name: Moncure Plywood,LLC 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 ED *OS ID *OS Description
GR2 I-10,I-9 32 Green Veneer Stackers
26 Veneer dryers and heat source(wood
burner)lbs/SF,(Softwood)
27 Veneer dryers and heat source(wood
G-24 ESO1-A,ES burner)HAPS lb/mmBtu,(Softwood)
ES09,ES 10 Veneer dryers and heat source(wood
30 burner)Ibs/SF, (Hardwood)
31 Veneer dryers and heat source(wood
burner)HAPS lb/mmBtu,(Hardwood)
G-25 I-4,1-5 5 Ink and painting operations
G-27 ES14,ES17 20 Woodwaste Transfer(Rechipper)
system
ES-11 16 Green wood fuel storage silo
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)
ES15 19 tongue and groove operations
ES 16 9 plywood hog
ES20 18 Vat Operations:Heating of Blocks
ES21 33 End Sealer Spray Booth
ES22 34 ITongue and Groove Saw
3

I-1 2 Bark Bogging operations_:.
. 1711 25 Hammer hog truck dump-no controls .
— 24 Dry Waste truck dump
I-2. 3 Core chipping and handling operations
I-3 4 Green veneer hogging in operations
I-6 6 Plywood.surface patching ... ..
! 1-7. 7 Maintenance parts washer .
I-8 8 Veneer diverter exhaust cyclone
IES.19 11 250 horsepower diesel—.fired water
pump:
I _
_
L.
i
r
f ..
- 4

Facility Total CY 2012 Emissions Summary
As entered in AERO
Facility Name: Moncure Plywood, LLC 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 2012
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 2012 1 2011 % Difference
Criteria Pollutants
Actual Emissions Tons/Year
Pollutant CAS 2012 2011 %Difference
CO CO 27.29 25.78 5.8572545%
NOx NOx 38.94 41.08 —5.2093554%
PM TSP TSP 57.64 49.68 16.022541%
PM 10 PM 10 57.64 49.01 17.608654%
PM2.5 PM2.5 52.93 46.9 12.85714%
S02 S02 3.55 3.74 —5.0802155%
�7�VOC VOC 1 51.77 43.05 1 20.25552%
Hazardous Air Pollutants HAPS and/or Toxic Air Pollutants TAPS
Actual Emissions Pounds/Year
Pollutant I CAS 1 2012 1 2011 % Difference
Pollutant Grou :Antimon Compounds total mass, inc elemental SB Gr up Sum:2.24355
Antimony Unlisted Compounds(Specify SBC—Other 2.24355 2.35942 —4.9109526%
Component of SBC
Pollutant Grou :Arsenic Compounds total mass of elemental AS, arsine and all inor anic compounds) Group Sum:.21016
Arsenic Unlisted Compounds (Specify ASC—Other 0.21016 .22101 —4.9092793%
Component of ASC
Pollutant Group:Beryllium compounds Total mass Group Sum:.31239
Beryllium Compound,Unlisted(Specify
BEC—Other 0.0 Not reported N/A
Component of BEC
Beryllium metal (unreacted)(Component of 7440-41-7 0.31239 .32853 —4.9127975%
BEC
Pollutant Grou :Cadmium compounds total mass inc elemental metal Group Sum:7.51694
Cadmium Metal(elemental unreacted, 7440-43-9 7.51694 9.53399 —21.156408%
Component of CDC
Cadmium Unlisted Compounds (Specify CDC—Other 0.0 Not reported N/A
Component of CDC
Vollutant Grou :Cobalt compounds Group Sum:1.84596
68

Cobalt Unlisted Compound(Specify COC-Other ..... 6 1:9413 -4:911143%
{ Component of COC) ....
Pollutant Grou :Lead and Lead compounds Group Sum:13.63171
Lead Unlisted Compounds(Specify and
�i Com onentofPBC PBC-Other i3:63171 14,33573 =4:910943%
` Pollutant Grou :Man anese compounds:G'r
oup Sum:454.3904
Manganese Unlisted Compounds(Specify
MNC-Other 454:3904 477:8576 -4.9.109173%
Component of MNC
ollutant'Grou :Mercu Compounds-all total mass 'inc H .Va or Group Sum:.993.98
Mercury Unlisted Compounds(Specify
HGC-Other 0.0. Not yeported N/A
Component of-HGC
Mercury,vapor(Component of HGC 7439-97-6... .. 0.99398 1.04531 . .-4.910508%
ollutant Grou :Nickel Compounds,,:suni total mass,inaeleriiental Group Sum:9.3718
�
Nickel Unlisted Compounds,(Specify
Component of NIC) NIC-Other 0.0 Not reported N/A
Nickel metal :Coin onent of NIC. ::. :: 7440-02-.0 ::. .. 9.3718 ... ::: : 9.85582 ... .:- .: -4.911%
Pollutant Grou :Chromium .VI Soluble Chromate Compounds Component of CRC Group Sum:.99398
Chromic acid(VI)(Component of So1CR6 7738-94-5 0.99398 .78816 26.113983%
:CRC .
ollutant Grou cChlorinated Dioxin Cornounds of interest as ..HAP or TAP Group Sum:0.0
Hexacl?lorodibenzo-p-dioxin 1:,2,3,6,7,8 5 7653-$5-7 0.0 Not reported N/A
(component of CLDC ... ..
...
Pollutant Grou :Chromium-All/Total Inc Chromium VI categories,metal and Others Group Sum:5.96387
Chromic.acid(VI)(Component:of SoICR6 7738-94-5 0:99398 78816 26413983%
CRC
:Chromium Unlisted Compounds(Specify CRC-Other 4.96989 5.22657 -4.9110603%
.Com,onent of.CRC)... .
? ollutant Grou :Pol c clic Or anic Matter S ecif c Compounds from:O A PS for TV GroupSum:28.28819'
. . .... . . ....
L! :Benzo(a)pyrene(Component of POMTV.
50-32-8: 0.7384 77653 4.9103117%:
.POM7)
LNaphthalene(Component.of POMTV 9:1-20=3 27.54979 ...28 97313 -4;9126205%
... Pollutant Grou :Pol .c clic Organic Matter 7 PAH Compounds for NIF Group:Sum:.7384
" enzo(a)pyrene:(ComponentofPOMTV
PO1V17 50-32-8 0.7384 .776.53 =4.91.03-117%
...,Acetaldehyde ...: 75. 07. 0 5051.538 3652.77631 38.29311%
.:Acrolein 107-02-8. 371.037:.. 282.77879::. 31.211046%::
Benzene 71-43-2 216.52573 168.95021 '28.1:5949%
Butadiene, 1,3= 106-99-0 0.0 . Notre ported :N/A
CFC-11 Triehlorotluoromethane - ::_ . 75-69-4.,. :-: .: 11.64376... ::. 12.2451 ... ... .. 4.910865%-
1 Carbon tetrachloride.. 56-.23-5 12.77973 13.43975 4.9109535%
Chlorine ::: 7782-50-5 224.35526 235.9421.9 -49.109187%
Chlorolienzene :::.. 108-90=7 .:::.. 9.3718: 9.85582 :,. : : :. -4.911%
Chloroform 67-66-3- 7.95183 8.3..625.1 4.9109635%
Cumene.::. : ..:98-82-8 2097.913 2274.51 -7;764174%
Di 2=eth lhex :1 hthalate EHP :. . 117-81-7 . : : 0.01335. .01403 4.8467603%
Dinitro henol,2,4-
51-28-5 : 0.05112 _: 05375 4.893021%''
Ethyl benzene :.. :: ...100=41-4 8 80382 9.25849 -4:910844%
Ethyl chloride chloroethane 75-00=3 :: . : 55.38615 59.8505 77.4591656%
Eth lene dichloride 1,27dichloroethane 107-06-2 86.01755 . . 92.7635 7.2722015%
- Fluorides sum of all fluoride:compounds) 16984-48-8 :0;0. Notre :orted ...N/A:
i
69'.

i
Formaldeh .de::. :: ... 50-00-0 ...2280.333 210:0.20631 8.576936%0
... :. H dro en chloride. h drochlorieacid . .. 7647-01-0-.. .. 159.03664 .:. . 5674.559 -97.19737%
.... . _.....
::Methanol 67-56-1: 11960.943 9786.388 22.220207%
-, Methyl bromide:::: .74-83-9 833033 9:1.2935 -8.3.14067%.
Methyl chloride. . .... 74-877-3 6.53.186 6.86921 -4:91.10436%
Methyl chloroform' 71-55-6.: : 8.80382::. . 9.25849:..: : 4.910844%:.
. .
. . .Meth 1 eth 1 ketone . 78-93-3 318.78476 307.8965 3.5363326%
Methyl isobutyl ketone .1.08-10-1 645.569 766.6485 -15:793357%
Methylene chloride 75-09-2. ::: .: - 74.7271... ::: . 81.1065 ... ::. :: .-7.8654633%
{ Nitro henol,4-.. .. 1.007702-7 0.03124 .03285 4.90107%
Pentachloro henol :: 87=86-5 0:01448 .01523 -4.924489%
. . .... . . ...:
Perchloroeth lerie: .fetrachloroeth lens: 127-18=4.::.:: 10.79177 .: 11.34912 4.910955%
. Phenol 108-9.5-2 . . 1476.73 1599.6025 -7.681443%
Phos horus Metal,Yellow or White :.772344-0 7:66784 ::.8;06384 -4.9108105%
Polycyclic Organic Matter-(Inc PAR
. .
r . :. .
dioxins, etc.NC AP 42 historic amorphous POW: 35.50395 37.33861 4:9135823%.
lob .. .
Pro ionaldeh'de . 123-38-6 232.9338 242.1.51 3.8063827% ..
Pro o. ldne dichloride 78-87-5.. : 9.3718:::. : 9.85582 ::: : 4.911%
Selenium Coin ounds --SEC 0.79519 .83625 4.9100184%
Styrene 100-42-5 152.0647 136.959 11:029358%o
..Toluene .. 108-88-3. :.- 320.83435. : . 239.68256 33.858032
Trichlorobenzene, 1,2,4-. 120=82-1 1.60.2818 173.576 7:6590104%
Trichloroethane 1,2 79-00-5 0'.0' N6t re orted N/A
Trichloioeth lene .. 79-01-6 .::.:: 8.51982 8.95983 :... : : :. -4.91091976/o..
00657 -4.8
Trichloro henol,2,4,6- 88-06-2 0,00625 7,0626%
Vinyl acetate': 108=05-4 8.19 871 -5:.9701543%
i� Vinyl chloride 75-01-4 54:69188 .::.:: 59.4095 7.9408526% .
X lens
1330-20-7 338.85114: 295.97815 _.:14.4851870/(
{ X lene, o 95747=6 0:0 Not re'orted1/A '
L_
.. .. ..
..: .:
.. :...
. .... .... . .... .
.. .. .. ..
T 1
..., ..
j
. .. ... ..
... ... .
..:: ... -. .. .. .. .. 70

Moncure.Plywood LLC
Facility-Wide Summary of Actual Emissions
2012 Air Emissions Inventory
i
URS Project No.31828920
j
Compound Emissions.: Emissions^I lb/ r
tons/.r.
1. 54;573r 27,29., b - --
NOx .t.w a' t :r, t - 1• "�77'886 38E94r is
11'4;739' Sr7,d37 �•
f PM10r
1`05;342._ G 5267s : .'• _,
m, i. 1'03.072;
q 7r108t
Emissions Emissions DeMinimus
Compound Ned to
` Report in
lb/yr ton/yr (lb/yr.)„
:AEI?., .
ACeta7deh°de,(TH)1t c. e t 5;051�54' �� ;2-53Et00,' :fi >,�lOfl r v Yesr::
Aceto henone(H) 9.09E-04..: 4.54E-07 100 No
ACrOlein:+.' i..-7 is .G E T _ f�''a,i i _ d3i7? 04� r r A ' 41 ;�k '+' l01 p.i 44r '{ � SL::n 1 .u:,�.�� _186E�01: _..-w.LO ._1'
Antimon &Compounds (H) 2.24 1.12E-03 10 No
Atsetuc4&,,Com oinds,.(91I)fi " " ^_ r °„+d Q:211. .,,.°:3 .1 OSE�04! S i©10Y� `,", , Vii`5-J
Benzene-' ,;7fY6__ r� r ;108E013 ii 1�� ".5Yes4n?1
m.,
Benzo(a) eue:(T)
-. :. . 0.74 .... ,3.69E-04 . . .... 1 :: . : No
Beryllium Qom ourids(T/H) 0.31 1.56E-04 1 No
I ladminm'.Com-QUI1dSr i ,i-+ , � ,«. � r rg � w i r Y, r •x r a 1 r`=���+ ,y ,.. .�
a �/H).a...; :..,,:•.;�:i!xa,_�._�.iT16`,k.,;"�.�p ,es'.
Canbon,tetractiloi le,;(.1 <.y»,.,sY.»:,: it».2> :�_ :.�1�2.7$n :»_..lt., r 'IV Yesi" �(i
GhloiRnet'1 Hi1 ai m.,r - -n r r » r r.
k,.u:�FNa !.�;:12E.01�.�'a, v.`r.f100A�•'k r ! .1'<CS�'•,•�a
Chlorobenzene(TH) '9.37 4.69E-03 10 No
Chloroform-(TH) 7.95 I I 3.98E-03 100 . . ...: No
Chr
omium`-0tliez com�8si i L+' '_��` �C � K4!9 _,_
Glicomiiuxi'`?ICom" und's"CPS_ h _ 1, =099 Yes:_'J
Cobalt com oundsl ) iR .1:$5. r _r9'.23E.04. lr Yesi
CumarielU5E+0(25'r ,t z -:.
-t,.: « 00 .v: .�Ysess,
Dinitro henol;2,4(H) "' 0.05 2.56E-05 :: . : 0.1 No;: .
Di(2=eth lhex 1) hthalate:(DEHP)(TH) :::O:Ol 6.67E-06 " 10 No
Ethyl benzene(l):. 8:80 ' 4..40E-03 100... . No
EIIt llchloride+(chlorbethane t'(H' s ki 55.39't y 2}77E
Eth lene'di'ehlonde�'c z.,,.,' .�,.: t•- ' ",�„ll+86i02x„,..,, a �, ,,.,4.30E-02._:.., x.
---
ormalde)i.',de;G'Ii .r n ,. ;... 2,28p33, 00': . 7a10; :;;_x,,. ;1�14E+ , t
- Hexachlorodibenzo- dioxin 1,2,34,7,8(T) 1.18E 07 1.39E 10 0.00001 No
H.d o en'chlonideE.(TH)i 15- } 0041 7 95Er02` ' 100 i_ Yes `
•[' ,-
I3.632
6:82&03;�
_..._
„
2:7,E,01:
IVlerc Com oiiiid:r rIH)l,. „ [ 3:99; I r 4"97E;;04;" Qt001„ Xes
1 Methanol`(d-I' .:h ..
.�.
^; A.1�i11960T9'4+ ..,W `1000T
d i„ '89tr7U! `"; 419E 02', - _- ;__i eth lilrotm e, �'. 11 Yies`,`.
Mbtfi D chlondei H+1 !. y: ;,_6:53;__.• i i"
» _31.17E,03_ a. i T',es; !-- _ -__. _ _._
� Meth:l chloroform(TH :::I . . ...8:80:: 4.40E=03. :;': 100 No
etli 1(et6 7;ketonel; ),-- a . (•-__ 3,1%78!s- F 159E 0,1�. _,t i_ ,1,00-_ _Yes ,
- 161et1i`IPlsobu 1 I{etone _� „,H� � ,:,�u t,;.•,� 645�5,7,;. `:;� 323E'01° �,1+, ,'ti101.�. ��. _Xes '�
Meth lntielchlon`de;(rTH) 7„4+73 +,� '`.r,. _,, 3�:74E`_'02 Yes;', "
y
N27sS5t, F; 9 LL 1:3,8Er02 ; , ti,�;t.li-':�'?3 Yes.;�1
� F K +
�,x° 3
Niek6FQ,b n ounds;(rT _ ,•_; 9?3�If- ,�:_ 469�,.Q __til Y,es a
Nitro heriol,4-.(H) 0.03 1;56E-05 . .' 10 :: . No
Pentachloro heriol(TH) ::: 0.01 : : : 7.24E-66 -:I: = No
Perchloroeth left(TH): 10.7.9-. 5.40E703 ... 100 • ' No ...
{i�'i-"' -iJ s F" `xc,rs rs r trG" vsg .
Plienoi;rTl1 �nk ,.,u �a g_.a t!ta .: . G 738EO..l�i :i� .. � 100 Xes,
1476 73 + .n
- Ptios horus:MetalEl'ellow�o`r�Whre_ j , Y1'es
Pol chlorinatedbi hen"ls (TH 2.31E-03 : 1;16E=06 10': : : No
Pol c cic;Or anicIlTatter t(f3) .t; �tr !'1L F1 35=SU1, 1�7f7E 02 _,,.� ;'.li
m •� w-±-;'Yv - �15"+'t ,• i --. 6 a.l rKl.4 j y w+-.0 e
;ro ionaldih.dei(I �S, ` �n � ,s h f t ?2 2:9. L + ti t1 1 16E�Q1�.?�,Leg Yes
Propylene dichloride(H)' 937 4.69E-03; ' 10 No
Selenium com ounds(H) : 0.80 3:98E-04 10 ::'. No
{ ... ..

. . . Moncure Plywood LLC
'Facility-Wide Summary of.Actual Emissions
2012 Air Emissions Inventory
j URS Project No.31828920
Nee dt
)� Compound Emissions Emissions DeMinimus, Report in
Ib/yr ton/yr (Ib/yr)
L_ AEI?
a "K.:h 'arm a c — r > •LF:, x s.S. 1 x r ;rr ene,,TH) ,.�� ,. :,..,b , :a •b :�,�;�,•�_,1.>52 04S .. r �.-,�ai0E,Q2;?°;''' :' 1 Q0: Yesi�'-,
etrachlorodibenzo dioxin.2 3 7 8 (TH) 244E 06 1 22E 09 _ 0.00001 No
1:-
:.plume -Hi L 3 - a ._ F�� 3219 831 a _..t.E z 1.60E Ol.- 1 1'00' ',j 3 Yesi4 �4
nchliir''oben�zene,r7 2;4.a 1I �_° " �:1602$L_ G� r$'.0 Ea02i fii. a;1b.0;,,LI'2�LI YesiZ
richloroeth Iene(TI4) 8.52 :. 4.26E-03 :: 1000 No
r-- richlorofluoromethane(CFC 111)M 11."64' 5.82E-03 100 No
Trichlorophenol,2,4,6 (H) 0.01 3.12E-06 - 1 - No
- Vin'I acetate(H :;:.'i 8.19 :: : : 4.10E-03 100: No
{ ,:F ,, '.;_54469 _`_;P` ,: 2;73EL02,_.. �"`i a`013 ��E1�Xes�__.i
win•IieliloridR e,.i d. E�.1�_ f.. �__ 4G �� F
JX�ffirk TH)fh_i LL = _Il'bI a _4L 3$85,?a „ 169E 01� ..6 _� 1.00t Yes�i "
_j

As entered in AERO
Facility Name: Moncure Plywood, LLC 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 2012
1. Emission Source ID (from permit) or Group G-24 consisting of ES01—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 —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 2012: 46285000 FT2/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#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
09A VERTICAL STACK 66 1 350 155 7304.2 Veneer drver ery
09B VERTICAL STACK 66 1 370 100 4712.38 Veneer dryer erp
09C VERTICAL STACK 66 l 340 150 7068.58 Veneer dryer er
09cool VERTICAL STACK 46 4 107 35 26389.37 Veneer dryer erp
10A VERTICAL STACK 66 1 350 155 7304.2 Veneer dryer er
I OB VERTICAL STACK 66 ] 1 370 ]00 4712.38 Veneer dryer er
l OC VERTICAL STACK 66 1 1 340 150 7068.58 Veneer dryer erp
I Ocool VERTICAL STACK 46 4 105 35 26389.37 Veneer dryer er
7

Operating Scenario: OS =
..2...6::: . Emission.Source/Group ID .G-24
...
....
10.;Operating Schedule; (Source/Operating:Scenario that best characterizes:Calendar Year 2012)
Hours per.Da 24 . Days per Week 7 Weeks er Year..Yearj 52
11:.Typical Start&.End Times For Operating Scenario: Start: 0 End: 2359...
. . ....
12. Seasonal Periods Percent Annual Throu h ut.
an4eb .+Dec o arch—May o : une—Aug. o �Sept.7��ov. o
012 25% 012 25/0 25/o . 012 25/o
0:12.
13::Actual Emissions p er Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used:
Emissions= Emission Control
GHG
CAS ::GHG Estimation Efficiency. : Emission
.
Pollutants Pollutants Method Code: (Net after Factor Ef Control
Tons/Year .:: :.See Instructions all controls
2012
Criteria Emissions- mission Control
Pollutant Criteria Estimation Efficiency. : Emission
(NQS) Ef Control
Pollutants
Code Method Code. (Net after, Factor
Pollutants ..
" (Tons/Ye :: (See Instructions) all controls)
.2012
CO. CO 4. 13.89 04 0 0.0006 : AFTER
NOz. :.. : NOg .: 08 :: ;:0
TSP `. . _..: . TSP. . ...: 08... .. 65 .
PM10. PM10 08 65 ..
PM2.5::: : PM2 5.: 08 65.
:77-
S02 S02. . ... .: D8 0..:
VOC VOC 24.76 04 0 0.00107 : AFTER
HAP/TAP . Emissions Emission Control
Pollutants (IriAlphabetical CAS HAP/TAPS n Estimation Efficiency Emissio EF Control
(see instructions) Method Code (Net after all Factor
Order) (Pounds/Year)
See Instructions): controls)
2012
i Acetaldehyde ..:: 75-07=0 3934.225 08 0..:
0.000085 • AFTER
P Acrolein -107-02-8 ::. '29.6.224 :.08:::': 0 0:0000064 -AFTER
Benzene: . : 71-43-2: 1 66.626 08 0.0000036 AFTER
1 ` Cumene 98 82
. ..
' 08 . 0..: 0.000013 .:. AFTER
... .. 8 ._ 601.705 .
::Ethyl;chloride
chloroethane.
75-00-3 16.19975 08 0 3.5E-7 AFTER
Ethylene dichloride
107=06-2 ... 25.45675 08 . 0..: _ 5 5E 7 AFTER
'` i,2-dichloroethane •
:15704: 050-00-0 0:Formaldeh de 1 000025 AFTER
Metha,nal :; .: 67-56=1 : 1666.26.:: ; : .: 08 :0 .: 0.0:00036 AFTER
Meth 1 bromide 74-83=9, 2:3.1425 08:: . : 0'' : . : .5E-7 AFTER
Methyl ethyl ketone 78-93-3 :::111.084 08 0 0:0000024 AFTER
Meth l isobu.. l ketone 108-10-1: 46.285 .. 08 :::0 0.000Q0 L: . AFTER... . ::
Methylene chloride 75-09 72
AFTER
... — .. 2.1.2911 ...: .08... .. . 0 �' . 4.6E=7

Phenol ... : : 108-95-2 ... 361.023 08:: : 0 : ::0.:0000078 AFTER
Pro ionaldeh .de. 123-38-6 83.313. A. 0.000001.8 . AFTER
styrene::,: a 100=42=5 87.9415.: 08 0 0.0000019 AFTER
:..Toluene 108-88-3 263.8245 08:.:. 0 0.0000057 AFTER
Trichlarobenzene, 1,2,4 120-82-1 46.28:5 08. . ...: 0 .0.000001 `AFTER
Vinyl chloride .: 75=01-4" .: 15.50548:: : 08 0.: 3.35:E-7 AFTER::.
+
X .lene 1330-20-7 210.59675 08:; . : 0 :0.00000455 AFTER
mam
a .. . .
I '
10

As entered in AERO
Facility Name: Moncure Plywood,LLC 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 2012
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 —27/Veneer dryers and heat source(wood burner)HAPS lb/mmBtu,
(Softwood)
4. SCC Number/Description: 30700740/Plywood Operations ; Direct Wood—Fired Dryer: Non—specified
Pine Species Veneer
5. Throughput/units in 2012: 111838 E6BTU/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-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 ery
10A IVERTICAL STACK 66 1 350 1 155 1 7304.2 Veneer dryer erp
1013 VERTICAL STACK 66 1 370 100 4712.38 Veneer dryer er
1 OC IVERTICAL STACK 66 1 340 150 7068.58 Veneer dryer er
11

d
Operating Scenario: OS—27; Emission S:ouree/Group M G-24
10. Operating Schedule; Source/O .eratin Scenario that best characterizes Calendar Year 201.2
Hoursper.. Day* 2 .. Pays er 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—Fe ti +Dec o o ' une=Aug. o Sept. Nov. o 25/o tich—May. . 25/o . 25./0 01225/o0122. : 012
.... .
.11. -Actual Emissions.per Pollutant Listed
Attach.calculations and documentation of emission:factor's or other estimation,methods used.:
Emission.
Emissions-: .Estimation Control .
GHG CAS GHG Method fri iency Emission:
f Co
E
Pollutants
: Pollutants ' Code::: (Net after
Control..
:... actor
:(Tons/Year) all controls)
1_.�. . (See:. . _..
Instructions .
2012
Emission
Emissions Estimation Control
:Criteria :
NAA S
Pollutant Criteria Method. :Efficiency Emission
( Q ) Ef.Control. . ..
Code Pollutants :: Code -(Net:at'ter Factor
Pollutants
(Tons/Year) . . (See all controls):
--. . ... .. Instructions . .
.2012
CO .:!CO, 08 0. ..
NOz NOg :15.31 08.:: 0
TSP.: TSP 13J4 08 . . ... 65 AFTER
PM10 PM-10 13.74::: .:08 :.::65 : :'AFTER
PM2.5 PM2.5... :: .13.46 08 65 .AFTER
:S02 : S02 1.4 0& 0 0.02.5: AFTER
VOC: :08 ...
.mission..
' ' Emissions Estimation Control
I h HAP/TAP CAS. Emission
Method '''Efficiency Efficiency E n E�.__.. HAP/TAPS: :: .. E:Control .
:Pollutants (In Alphabetical Order) (seeanstructions) Code (Net after all Factor
: Wounds/Year). .
contro
ls)
See.::.:. ... ..
Instructions)
2012:
Antimony Unlisted Compounds.(.Specify
SBC—Other 10.88352 08 .::;: _ 0 0.0000079 AFTER .:
Component of SBC
Arsenic.Unlisted Compounds (Specify
ASC Other 0.08276.. ::: :: :02 0::: 7.4E-7 ... :AFTER
Com onent of ASC
Benzo a rene(Component of POMTV:
OPY :
P .:50-32-8 029078 08. 0 0:0000026 AFTER:: :
f. _. .. `:POM
Beryllium metal(unreacted)
7440: 41-7 0.12302: : 08 0 0.0000011 :' :AFTER
(Component of BEG
CFC-11 Trichlorofluoromethane �- :75-69-4 :4.58536 08: : 0 0.000041 AFTER
7440. 43-9 0.45854 .: ::: 08 0; 0.0000041: .. AFTER
; i
13. :.

Cadmium Metal(elemental:unreacted,
Component of CDC
Carbon:tefrachloride 56-23-5 5:03271 08 : 0 0 000045 AFTER:
Chlorine 7782-50-5 �88.35202:: . : 08 Q. : 0:00079 :AFTER
Chlorobenzene 108-90-7 3.69065` : 08
-f Chloroform ::::: 67-66-3 3:13146 08.::: 0 00.0.0028 AFTER. .
= ..Chromic acid'(VI).(.Component of-
7738-94-5 0.39143 ,:: :: 08 .:0::. 0.0000035 AFTER
So1CR6 CRC :: :.
Chromium Unlisted Compounds
CRC-Other... :::1:95716 08 : 0 0:00001.75 AFTER. :
(Specify Component of CRC ::
i Cobalt:Unlisted Compound:(Specify
Com onent of COC
COC=Other 0.72695 08 :0 0.0000065: AFTER
Di 2-eth lbez 1 hthalate EIR: 117-81-7 :: : : 0:00526 08 : 0 :::4.7E-8 AFTER
Dinitro henol 2,4 51-28-5. 0.02013 :: . : . 08 0. : L8E-7 ::AFTER
Eth 1 benzene: 100:-41-4: 3.46699: 08 0 0.0.00031 AFTER
ir' r H dro en chloride: h .drochloric acid : 7647-01-0 . . :62:62928 10 ::. :: 0 0:0005.6 AFTER:
Lead Unlisted Compounds.(Specify and
Other 5.36822 08 0.000048 TERPBGCom onentofPBC F
Manganese Unlisted Compounds .
S eci Come onent of MNC MNC-Other. : 178.9408 08. 0 :::0:0616. AFTER.
Mercu: va or Com on6f of HGC 7434 9:7-6 0.39143. : :: -. 08 .- 0: -: 0.0000035. RAFTER
..Methyl chloride , 74=87-3. . ..2.57227' 08 ... .. 0 0.000023 AFTER
Meth 1 chloroform . 71-55-6 ':J3:46698 Q8 : 0 :0.00003:1 AFTER
Naphthalene Com onent.of:POMT 91-2:0-3 10.84829.:: :: 08 0::: 0.000097: AFTER
t ..
Nickel metal Com onent of.NIC 7440=02-0 3.69065 08 0 0.000.033 AFTER ..
Nitro henol 4- 7 :100-02-7 :: : -a.0123 08: 0 1::1 E-7 AFTERS
;: . Pentachloro`henol.:: 87786-5 . 0.0057 : . : .08 0 . 5:1E-8 AFTER
I Perchloroeth lene tetrachloroeth lene 127=184- 4.24984: 08 0 0.600038 ;AFTER
Phosphorus Metal-Yellow or White:: : 7723-14-0 . . ::3.01963 08. ::: :: 0 0:000027 AFTER::
Polycyclic Organic Matter(Inc,PAH;
Aiozins,.etc.NC AP:42 historic ;POM 13.97975 08 0 0.000125 : AFTER
amor .hous lob
Propylene dichloride - .78-87-5 3.69065 08: : 0 0.000033 AFTER
::;Selenium Compounds: SEC: 0.31315.. :: :: 08 0: :: 0.0000028: : 'AFTER
u Trichloroeth lene 79=01-6-: . .3.35514 `08 ... .. 0 0.00003 AFTER
....
Trichloro henol,2 4 6- -:88-06-2 :0.00246 08 0 : 22E=8: AFTER.
p.
:-:..
_. _..
ms
1:4

As entered in AFRO
Facility Name: Moncure Plywood, LLC 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 2012
1. Emission Source ID (from permit)or Group G-24 consisting ofES01—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 —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 2012: 71248000 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 inpen-nit)
1 CS-1 CD02 Multic clone 720 six—inch diameter tubes
i 1
9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
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 l 340 150 7068.58 Veneer dryer er
09cool VERTICAL STACK 46 4 107 35 26389.37 Veneer dryer erp
10A IVERTICAL STACK 66 1 350 155 7304.2 Veneer dryer er
1013 VERTICAL STACK 66 1 370 100 4712.38 Veneer d er er
IOC VERTICAL STACK 66 1 340 150 7068.58 Veneer dryer er
I Ocool VERTICAL STACK 46 4 105 1 35 26389.37 Veneer dr er er
15

Operating,Scenario: OS —30: Emission.Source/Group ID: G=24;
.. .
10..Operating Schedule: (Source/Operating:Scenario that best characterizes:Calendar Year 2012)
Hours per.Day '( 24 )- Days per Week ( 7 ) Weeks'per Year ::( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent:Annual Throu h ut: .
an=Feb .+.Dec o arch—May o . une—Aug.. o Sept..—Nov. o .
25/0 25/0 012 25/0 012 25/o
012
4� 13. Actual Emissions per Pollutant Listed
{ Attach zdkulations and documentation of emission factors or other estimation methods used-.
Emissions-: Emission Control
GHG CAS
:GHG Estimation Efficiency. Emission
Pollutants f Control
Pollutants Method=Code: (Net after Factor
Tons/Year .See Instructions all controls
2012 .. .
Criteria Emissions- Emission Control
.. .. .
AA S Pollutant Criteria Estimation Efficiency. Emission
(N Q ) .. Ef Control
Pollutants Code Pollutants Method Code: .(Net after Factor
:(Tons/Year),. (See,Instructions), al:controls)
2012.
CO CO 13.39 04. 0 0.000376 AFTER
NOx. : NOx:: :: 08_ . . 0 .
TSP. : ...: TSP .
.08... ... . 6.5..
_ 1
PM10 PM10 .08: . .. 65
.. . .
PM2.5::::. 08
65
SW S02. . ... 08. 0
VOC VOC 5.59: :04 0 0:000241 AFTER
I
HAP/TAP:. Emissions,
Emission Control
CAS Estimation Efficiency
Emission
Pollutants (In Al habetic. HAP/TAPS ctor
PEF.Control
(see instructions)' Method:Code (Net after all -:: :: Fa
Order) (Pounds/Year)
See Instructions): controls)
2012 . ..
Acetaldeh de -.-- 75-07-0 370.4896 08... .. 0 ..0.0000052 AFTER
Acrolein 107-02-8 74:8104 08:: 0 0.00000105 AFTER
Benzene: _ 71-43 2:: 49.87M 08 0 7E77...
Cumene. 98-82 .8 1496.209 08 0... 0.000621
LJ
Ethyl chloride 75-00-3 .39.186:4 08 0 5.5E-7
chloroethane)
. ...... . .. ...
Ethylene dichloride
107=06-2 60.5608 08 0 8.5E-7
12-dichloroetliane . :
Formaldeh de 50-00-0 700.367.84 04 . . - 0 . . 0..00000983 AFTER
Methanol:':. 67=$6-1 676.856.::: 08 0 .: 0.0000095 AFTER::::
Methyl.bro 11mde 74783-9 60.5.608 08:.-.-: 0 8.5E-7
... ... ..
Methyl ethyl ketone 78-93-3 A 67.4328 08 0 0.00000235
} Methyl isobu.. .i:ketone 1 108-1.0:=1:. 160.308 ... : .. 08 . .0 0.00000225
Meth Jene chloride . 75-09=2 53.43.E .08... 0 7.5E=7 ... .. .
17:

r-,
10600l: IVERTICAL S'TACKI 46 4 105.. ::: 35 26389.37 Veneer dryer erp
j-.

Operating Scenario: OS—31::: Emission Source/Group ID .G-24
10.:0 Operating Sc4edule: Source/O ,eratin ;Scenario that best characterizes:Calendar Year 2012
P g . ( P g
Hours per.Pay' 24 Days per Week 7 Weeksper Year . 52
. .....
11..Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut;
... —Aug. Se t.-Nov.an=Feb +IIec une25/ 25/ 25%
25%.
012 012. 02
c .13. Actual Emissions per Pollutant Listed-:- .
Attach:calculations and docutrientation of emission:factors or other estimation methods used -
Emission
Emissions=: :Estimation Control
GHG CAS GHG Method fficiency. Emission: Ef
Pollutants Code:: : (1`I
Pollutants et after Factor Control
s/Y Tonear
( . .. . ) (See . . - :all controls)
0 Instructions
2012
mission
Criteria Emissions— Estimation Control
Pollutant Criteria Method. . .:Efficiency Emission
.
(NAAQS) Ef.Control
Code Pollutants::: Code (Net:after.: Factor
Pollutants:''
_(Tons/Year) ..-:(See-.. all controls)
. ... .. Instructions
2012
CO 08 ,0: ..
NOx : :23.57 08. ::: :. 0
TSP.: . TSP. 21.15 08 65 .. AFTER '. . ..
PM10 P1Vt10 : 21.15::: : 08 65 AFTER .
PM2.5 PM2.5 :,::20.73 08. 65 AFTER
:S02. S02 .2,.15 08 . . ...: 0 0.025.:. AFTER-
...... VOC
VOC .: 08 ::: 0:,:
Emission
E
Emissions
Estimati
on n Control
HAP/TAP CAS: Emission
fficienc
:Pollutants (In Alphabetical Order) (see:instructions) HAP/TAPS Coded (Net after all: Factor : EF C . ro
. (Pounds/Year). . ..
o contr ]s
.....' (See.::: : ) .. ..
_..
Instructions
. ...... 2012... ::
Antimony Unlisted.Compounds(Specify
SBC Other: 1.36003 08 0 0.000:0079 AFTER..
Com .omnt of.SBC
Arsenic Unlisted Compounds;(Specify . .
Component of ASC
ASC=Other 0.1274:, : : : 02 0 7.4E-7 ::: AFTER
::Benzo(a)pyrene,(Component of POMTV:
^! 50-32-8 : 0.44761 68: 0 0:0000026 AFTER :
TOM7.
.:.Beryllium metal(unreacted)
7440:' 41-7 0.18937' = , ..08 Q 0.0000011 'AFTER
I
Component of BEC
CFC-11 richlorofluoromethane 75-69-4 7.0584 08: 0 0.000041 AFTER
7440::43:-4 7.0584... : : :: 08 0:: :: 0.000041 .. :AFTER

Cadmium Metal(elemental:unreacted,
Component of CDC)...
Carbon:tetrachloride .. 56-23-5 .::: : 7:74702 08 ; 0 :0:000045 AFTER:
Chlorine 7782-50-5 136:00324:: . : 08 :0. : 0:00079 AFTER
.. :.
Chlorobenzene 108=90-7. 5.68115 : 08 0 0.000033: : ' AFTER
Chloroform 67-66-3 4.82037 08 ::: :: 0 0:000028 AFTER
Chromic acid(VI)(Component of
773811194=5 0.60255. :: ::: 08 :4 0.0000035. ::AFTER
. So1CR6 CRC :
Chromium Unlisted Compounds ::::,
CRC-Other.. : : 3:01.273, 08 : 0 0.00001.75 AFTER
... ..
(Specify Component of CRC
Cobalt Unlisted Compound:(Specify COC-Other 1.11901 08 0 0.0000065 . AFTER
Component of COC
Di 2-eth llie 1 hthalate(DER : 117-81-7 0:00809 08 0 .:4:7E-8 AFTER
-
UP)henol 2,4-_: 51-28=5 0.03099 .:: :: 08 .0.:: 1.8E-7 : .::AFTER
..Eth l benzene:. _ ._.: 100=41-4. 5.33684 08 0. ...: 0.000031 AFTER
::H dro en chloride h .drochloric:acid: : 7647-01-0.: 9640.736 10 0 000056 AFTER.
Lead Unlisted Compounds.(Specify and
PBC Other 8.26349. :: :: : 08 . . :.6 0.000048. . AFTER
Component of PBC
Manganese Unlisted Compounds.:: ::
MNC-Other.; _ :275.4496 08 : 0 0.0016 AFTER:
(Specify Component of MNC
Mercury,vapor Com :onent of HGC 7439-9776 0.60255: ; 08 0 0.0000035: : AFTER
Methyl.chloride 74-87 3 ::3:95959 08 :: . : 0 0.000023 AFTER
Meth* l chloroform 71-55-6 5.33684 08 0 0.000031 AFTER:
Na hthalene Com onent of POMT 91.=20:=3: 16.69913 : :: . 08 0: :. 0.000097. . ::AFTER
Nickel metal Com orient of NIC 5,68.115 08 .-. .. 0 0.000033 AFTER ..
7440.-02-0.
_ Nitro`henol 4- :100-02-7 : : : 001894 08 : 0 LIE-7 AFTER
- Pentachloro' henol; . 87-86=5 0.60978 .:: :: 08 0:.:: 5.1E-8 : .::AFTER
Perchloroeth lene tetrachloroeth lene 127=18-.4: 6.54193 08 0 . ...: 0.000038" :.AFTER
Phos horus:Metal,Yellow or White=:: 7723-14-0 :: : �4.64821 08: 0 :0.00002:7 AFTER:
Polycyelic Organic Matter:(fnc.PAR;
diozins;:etc.NC AP 42:historic POM 21.5195 08 :: 0 0.000125 :AFTER
_. .. amor hous. lob
Pro Tone dichloride 78-87-5 5..6.8.115 08 . . ...: 0 0.0000.33 AFTER
Selenium Com pounds .: ::SEC 0.48204: 08 0 0.0000028: : :AFTER
Trichloroeth lene .79-01-6 .:5.16468 08 :: . : 6 0:00003 AFTER .
Trichloro henol,2,4,6- .88-06-2 0.00379 08: : 0 2.2E-8 AFTER:
as a
i
::

Moncure Plywood LLC
Emission Source(s): Fluidized Bed Wood Boiler and Two Direct Heated Dryers
Source ID Number(s): ES-01,ES-09,ES-10,CD-02
Emission Point(s): EP-09a-d,EP-10a-d
2012 Actual Process Throughput: §Boiler operating hours/yr
27,381 ton wood/yr
283,995 MMBtu/yr
227,389 MMBtu/yr Green Wood
56,606 MMBtu/yr Dry Wood
71,248,000 sf/yr Hardwood
J6,Z85,000 sf/yr Softwood
117,533,000 sf/yr Total Plywood Production
172,156 MMBtu/yr Hardwood
111,838 MMBtu/yr Softwood ✓
Actual Emissions Summary:
Hardwood Softwood Total
Compound Emissions* Emissions* Emissions
P Emission Factor Units Ref. Emission Factor Units Ref.
ton/ r ton/ r ton/yr
CO 3.76E-04 lb/sf 1 13.39 6.00E-04 Ib/sf 1 13.89 / 27.3
NOx(dry wood) 4.90E-01 lb/MMBtu 2 8.41 4.90E-01 lb/MMBtu 2 5.46 13.9 !
NOx(green wood) 2.20E-01 lb/MMBtu 2 15.16 2.20E-01 lb/MMBtu 2 9.85 25.0
Total NOx 23.57 --- --- --- 15.31 38.9
PM 8.308 lb/hr 3 21.15 9.308 lb/hr 3 13.74 34.9
PM10 8.308✓ lb/hr 3 21.15 / 8.308 lb/hr 3 13.74 ✓ 34.9
PM2.5 8.14 lb/hr 3 20.73 8.14 lb/hr 3 13.46 34.2
VOC(as acetic acid-hardwood and inene-softwood) 2.41E-04 lb/sf 1 8.60 1.07E-03 lb/sf 1 24.76 33.4
SO2 2.50E-02 lb/MMBtu 2 2.15 2.50E-02 lb/MMBtu 2 1.40 3.5
Lead 4.80E-05 lb/MMBtu 2 1 0.0041 4.80E-05 lb/MMBtu 2 0.0027 j 0.0068
Emissions* Emissions
Ib/ r Emissions*
Compound Emission Factor Units Ref. Emission Factor Units Ref. Ib/ r Ib/yr
Acetaldehyde(TH) 5.20E-06 lb/sf 5 370.49 8.50E-05 lb/sf 5 3934.23 4304.71
Aceto henone(H) 3.20E-09 lb/MMBtu 2 0.00 3.20E-09 lb/MMBtu 2 0.00 0.00
Acrolein(TH) 1.05E-06 lb/sf 5 74.81 6.40E-06 Ib/sf 5 296.22 371.03
Antimony&Compounds (H) 7.90E-06 lb/MMBtu 2 1.36 7.90E-06 lb/MMBtu 2 0.88 - 2.24
Arsenic&Compounds (TH) 7.40E-07 lb/MMBtu 6 0.13 7.40E-07 lb/MMBtu 6 M53
0.21
Benzene(TH) 7.00E-07 lb/sf 5 49.87 3.60E-06 lb/sf 5 216.5
Benzo(a) ene (T) 2.60E-06 lb/MMBtu 2 0.45 2.60E-06 lb/MMBtu 2 0.74
Beryllium metal(T/H) 1.10E-06 lb/MMBtu 2 0.19 1.10E-06 lb/MMBtu 2 0.31
Cadmium Metal(T/H) 4.10E-06 lb/MMBtu 2 0.71 4.10E-06 lb/MMBtu 2 1.16
Carbon tetrachloride(TH) 4.50E-05 lb/MMBtu 2 7.75 4.50E-05 lb/MMBtu 2 12.78
Chlorine(TH) 7.90E-04 lb/MMBtu 2 136.00 7.90E-04 lb/MMBtu 2 88.35 224.36
Chlorobenzene(TH) 3.30E-05 lb/MMBtu 2 5.68 3.30E-05 lb/MMBtu 2 3.69 9.37

_ 4� J
r
r
p.
Moncure Plywood.LLC
Emission'Source(s): Fluidized Bed Wood'Boiler and Two Direct Heated Dryers
Source ID Number(s):ES-01,ES-09,ES-10,CD-02
Emission"Point(s):"EP-09a-d,'EP-10a-dq.
"
2012 Actual.Process Throughput: 8,399 Boiler operating hours/yr
27,381 ton wood/A
283,995 MMBtu/yr
:.. ::227,389'MMBtu/yr ...:Green Wood... ::
.. .
56,606 MMBtu/yr Dry.Wood
71,248,000 sf/yr. Hardwoodp.
46,285,000 sf/yr .:." Softwood
wr
117,533,000 sf/yr........ TotaT:Plywood Production
171,:B6 MMBtu/y. Hardwood
111,838 MMBtu/yf Softwood
Actual Emissions Summary:
Hardwood
Softwood , .. Total
Emissions* Emissions* Emissions*
Compound" Emission Factor Units Ref. Emission Factor Units Ref:
Chloroform(TH) :. :. "_ 2.80E-05 lb/MMBtu 2 -4 82 2:80E-05 lb/MMBtu 2 3 13 �7.95
Ili
/
Chromium-Other.com ds(H) 1.75E-05: lb/MMBw 2:: 3.01 1.75E-05 : lb/MMBtu:: 2 1.96 4.97
Chromic acid(VI.(T/H) ....:.. 3.50E-06:.. - lb/MMBtu 2 0:60::: 3.50E-06.^ :i: lb/MMBtu" .: 2 0.39 0:99
Cobalt compounds(H) 6.50E-06: lb/MMBtu: 2 .: 1,12: . 6.50E-06 lb/MMBtu : 2 0.73 -1:85
Cumene(H) 2.10E-05 1b/sf :5. 1496,21. 1.30E-05 lb/sf: 5 601.71: 2097.9.1
Dinitro henol,2;4-"(H) . ." 1.80E-07 lb/MMBtu . . . 2 . .0.03 1.80E-07 lb/MMBtu 2 0.02 0.051
Di(2-ethylhexyl) hthalate:(DEHP)(TH) : 4.70E-08 Ib/MM]3tu•-: 2 0.01 4.70E-08 lb/MMBtu 2, 0.01 0.013
Ethyl benzene(H) : 3 10E-05 'ali/MMBtu` : 2 5.34 3.10E-05 lb/MMBtu 2: : 3.47 8.80
Ethyl chloride.(chloroeihane):(H) 5-SOE-07 Ib/sf 5 39.19 3,50E=07 lb/sf 5'-: 16.20 55.39
Ethylene dichloride(1,2-dichloroethane):(TH) ; 7 8.50E-07 lb/sf :. . . 5 .60.56 5.50E-07 ]b/sf,, 5 . 25.46 86.02
Foxntaldehyde(TH)" 9.83E-06 lb/sf, 1:• 700.37 " _ 2.50E-05 lb/sf 1 1157,13 1857:49
Hexachlorodibenzo= -dioxin 1,2,3;6,7,8(T) 9.80E-13:.. lb/MMBtu 6 0:00::. :9.80E-13..:::..lb/MMBtu ::.. 6 0.00 2.78E=07
Hydrogen chloride(hydrochloric acid)(TH) : 5.60E-04 ]b/MNIBm 7 96.41: : :5.60E-04 lb/MMBtu :: 7 62.63 159:04
Manganese&compounds(TH) 1.60E-03 lb/MMBtu :2 ' ' 275.45"" 1.60E-03: lb/MMBtu 2 178.94 454.39
Mercury,va or(include in Mercury&Corn ds)(T/H) 3.50E-06 lb/MMBtu 2­ 0.60 3.50E706 lb/MMBtu' 2. 0.39 . ' 0.99
Methanol(H) 9.50E-06 lb/sf 5 676.86 3.60E-05 lb/sf . 5 1666.26 2343.12 "
Methylbromide(H)(bromoinethane) "".:;: : : 8.50E-07 :: lb/sf 5 60.56 5.00E=07 lb/sf 5" 23.14: 83.70 "
Methyl chloride(H)(chloromethane)" 2.30E-05 b/MMBtu 2 : ::3.96 2.30E-05 lb/MMBtu 2 .: 2.57 6.53
Methyl chloroform(TH)(l,l,l trichloioethane) 3.10E-05 lb/MMBtu 2 5.34 3.40E-05 Ib/Mq.MBtu 2_ :3.47. 8.80 :
Methyl ethyl ketone(TH) .2.35E-06. Ib/sf 5.:. 167.43 2.40E-. .: lb/sf 5 111.08 278.80
52
Methyl isobutyl ketone(TH) 2.25E 06-. lb/sf. 5 160.31 1.00E-06 lb/sf 5 46.29 206;59
Methylene chlonde:(TH)(dichioromethane) 7.50E•07•: lb/sf:: _ 5 :: 53.44: 4.60E-07: lb/sf" 5 21.29 74:73
Naphthalene (H) 9.70E OS ' lb/MMBtu .2 16.70 9.70E-05" lb/MMBtu 2 10.85 27.55
Nickel Metal(Component of Nickel&Compounds)"(T/H) :. : 3.30E-05. lb/MMBtu 2 5:68 3.30E-05 lb/MMBtu. 2 3.69 9.37
Nitrophenol,4-(H) 1:30E-07 ::Ib/MMBtu 2 0.02 1.10E 07 ]b/MNIBtu 2 0.01 0.031
Pentachloro henol(TH) .5..i:0E-08 lb/MMBtu 2 0.01 S.1OE-0$ lb/MMBtu 2,:.: 0.01:: 0.014 "
Perchloroethylene(tetrachloroethylene)(TH) :••" 3.80E-05 lb/MMBtu" 2 6.54 3.80E-.05 lb/MMBtu 2 -. 4.25 10.79
Phenol(TH) 3.75E-06 Ib/sf. 5 267.18 7.80E-06 lb/sf 5 361.02. 628.20

1 }
oncure Plywood I;LC
....... ... ....:.. ....... ..
Emission Source(s): Fluidized Bed Wood Boiler and T*o Direct Heated Dryers
Source ED Number(s):'ES-01,:ES-09,ES-10;CD-02
Emission Point(s):'EP-09a-d,'EP-l0a-d
2012 Actual:Process Throughput: 8,399 Boiler operating hours/yr
.. .. .
27,381 ton wooil/yr
283,995 MMBtu/yr :.
227,389.MMBtu/yr "...Green Wood.
56,606 MMBtu/yr Dry Wood "
71,248,000 sf/yr Hardwood
46,285,000 sf/yr ... Softwood "
117,533,000 sf/yr ....... Total.Plywood Production
.172.;156 MMBtu/yr.' Hardwood
" 11 T,838 MMBtulyf" Softwood
Actual Emissions'Summary."
Hardwood :Softwood Total
Emissions* Emissions* . Emissions
---. . ....
Compound- Emission Factor Units Ref. Emission,Factor Units Ref:
lb/yr 1b/yr Iti/yr
Phosphorus Metal,Yellow.or'White(H):• 2.70E-05 lb/MMBtu:" 2 4.65 2.70E-05 lb/MMBtu 2 3.02 7.67
Polychlorinated bi"Iienyls (TH)::: 8.15E-09 lb/MMBtu 2 i: 0.00 8.15E-09 _:: lb/MMBtu 2 0.00 0.002
....:.. Polycyclic Organic Matter (H)....:.. 1.25E-04:.: lb/MMBtu 2 21:52::: 1.25E 04," ;::ab/MMBtu ::. 2 ::.: 13.98 . 35:50
Pro ionaldehyde(H) 2.10E-06.:". lb/sf". 5 .: . 149.62". 1.80E-06 lb/sf, : 5 83.31 '232:93
Propylene dichloride(H)(1,2 dichloro ro ane) 3.30E-05 lb/MMBtu .2. 5.68 3.30E-05 lb/MMBm. 2 3.69 9.37
Selenium com.ounds(H). . 2.80t-'05 lb/MMBtu . . ."2 .0.48 2.80E-06 lb/MMBtu 2. 0.31 0.80
Styrene(TA) 9.00E-07 _ lb/sf 5 64.12 1.90E706 Ib/sf 5, 87.94 152.06
Tetrachlotodibinzo- diozin;:2,3,7,8 (TH) 8.60E-12 lb/MMBtu•" : 2 0.00 8.60E;12 lb/MMBtu 2: 0.00 2.44E-06 "
Toluene(TH).: 8.00E-07 Ib/sf 5 57.00 5.70E=06 lb/sf 5 263:82 320.82
Trichlorobenzene,1,2,47(H). 1.60E-06 lb/sf 5 .114.00 1.00E-06 Ib/sf 5 46:29 160.28
Trichloroethylene.(TH) 3.00E-05. lb/MMBtu 2 5.16 3.00E-OS 7b/MMBtu 2 3.36 8:52
Trichlorofluoromethane(CFC 111)_(T) :.::; 4.10E;05::." lb/MMBtu 2...... 7:06... 4.10E-05,...;..lb/MMBtu. :.. 2 4.59 11:64
TrichIoro henol,2,4;6-(H) ..
. 2.20E-08 lb/MMBu .2 - Too- 2.20E-08 lb/MMBtu :". 2 0.00 0;006
Vinyl chloride(chloroethene)(TH) 5.50E-07 lb/sf 5 39.19 3.35E-07. lb/sf: 5 15.51 54.69
Xylene(TH) 1.80E-06" lb/sf - 5 128.25 4.55E-06 lb/sf 5 210.60" 338.84
`Note: All emissions include emissions from.wood combustion and wood drying.::
References:::..
1- Stack Testing Data,1996
2-AP-42,Section:l:6 Wood Residue Combustion in Boilers .:. " .. ...
3<Based on Feb:"12,2010 stack test. PM 10 assumed to be equal.to PM. PM2.5 assumed to be 99%
4:-Interim VOC Me8itrement:Protocol for the Wood Products Industry-luly2007
5-AP 42,Section 10.5,Table.10.5-3,and related"information. '
6-NCASI Handbook,of Chemical Specific Information for SARA 313 Form R Reporting;2007"Reporting Year.
7-EF referenced in facility letter to DAQ:dated February 14,2003.(Subject:Reference request for Toxic Air Pollutants Modeling Study for the;Moncure Area)

As entered in AERO
Facility Name: Moncure Plywood,LLC 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 2012
1. Emission Source ID (from permit)or ES03—SMS—I
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
(1D 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 2012: 117533000 FT2/yr
(e.g. production or fuel use):
6. Fuel Information (1f 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-3 CD03—WWTC Woodwaste transfer cyclone 154 inches in diameter
2 CS-3 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 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
29

Operating Scenario: ... . . Emission'Source/Group ID:
OS-:21. .. .:
i
ES03—SMS-1 ..
w.
10::Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2012)
Hours per Day 24 ::Da s 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 z h ut: -
an—Feb +Dec ° arch=May,: ° une—Aug. o Sept.—Nov: °
012
25% : 25/o
° .:. 012 ...: 25 ° 012 . ... .. . . 4012 .
13. Actual Emissions per-Pollutant Listedq.
.Attach calculations:and documentation of emission factors or other estimation methods used.
ra
:. Emissions ::= Emission- : : : Control
GHG
GHG Estimation Efficiency EmissionCAS
Ef Control
Pollutants ....Pollutants Method:Code (Net after Factor.::: :
(Tons/Year) See Instructions all controls)
2012::::
), is :�� .. ... .. ... .... .... .. .. .. .... .
Emissions Emission .. : : :: :Control
Criteria
Pollutant ...: Criteria Estimation cien Emission.
Effi ' cy.
(NAAQS) Ef Control
Pollutants
Code : Pollutants Method Code (Net after Factor
(Tons/Year) ... . (See Instructions) . . .. all controls) .
i
2012
CO CO 08 ow,
NOz NOg 0. . ....
- TSP- .: TSP: 15.68:::: : 04 85 :AFTER
PM10-- PM10. . .... :: 15.68 q4. 85:::: AFTER .
P1%12.5 PM2.5 15.68 04. ; - 0AFTER
. . ....
sot_ sO2 08 . :. 0
- . voc voc 08 0
HAP/TAP Emissions Emission
CAS.::::: Estimation : : Control Emission
Pollutants (In HAP/TAPS: Efficient 'Control
(see mstrucfions) Method Code : Y Factor
Alphabetical Order) ... .. (Pounds/Year)' (Net after all controls)
. .....• See Instructions
2012
i .
pw
i ;

l {
to- Moncure Plywood LLC
,Emission Source.: Dr Waste Transfer System
Y Y . . :
:Source ID Number:: ES-03,CD-06
Emission.Point: EP-Q6
2012 Actual Process Throughput:
i
Hardwood Pl ywood Production 71,248;000 sf/yr
Softwood Plywood Production . 46,285,000 sf/yr
Emissions Summary:
Softwood Hardwood
Pollutant Emission Factor Ref. ;: :" Emission Factor 'Ref. Emissions
.6.60E-04 MAU .15E-05 Ib/sf 1 15.68 t y
PM_'10: 6.60E-04lb/sf 1 1.15E=051b%sf 1 15.68 y
_ PM-2.5 6:60E-04:lb/sf 1 1.15E-05 lb/sf : A: 1. 15.68 t y
16
References: a.. -
1. Emission factor from original-Title V Permit Application
i
i
:.:
L !
r

As entered in AERO
Facility Name: Moncure Plywood, LLC 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 2012
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 2012: 45326000 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-10 CD05 Ba filter 6,200 square feet of filter area
2 CS-10 CD03—WWTC Woodwaste transfer cyclone 154 inches in diameter
3 CS-10 CD06 Ba filter 7,095 square feet of filter area
9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP
(in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm) Description
Rectangle(L x
in 0.1 feet)
EP—WS DOWNWARD—FACING VENT 10 1 72 1 47.12 ERP for wood
sander
31

sw
Operating:Scenario: OS 11 aEmission Source/Group ID: ESO4
10..Operating Schedule (Source/Op.erating:Scenario that best characterizes:Calendar Year 2012)
Hours per.Da 24 Pays per Week .7 Weeks'per Year,: 52.
-1
11:Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu -h utc
an-Feb +_D.ec o arch-May o : une-Aug. o Sept...Nov. o ..:
25/0 25/0 25/0 25/0
012 012... ::: :: 412:
. . :
. 012
•13. Actual.Emissions per Pollutant Listed;
Attach calculations and documentation of emission:factors or other estimafion methods used.
�Eimissions- Emission Control
GHG GHG: Estimation . Efficiency Emission Ef Control
- CAS..
Pollutants; Pollutants Method Code ;(Net after Factor
Tons/Year See Instructions all.controls
. .... 2012
Criteria
'Emissions- Emission Control...: '
NAA S Pollutant::, Criteria.. ::: : Estimation... : : :: Efficiency Emission
( Q ): Ef Control
Pollutants
Code . . Pollutants Method_Code (Net after Factor .
(Tons/Year) (See:Ipstructions) all:contcols) .:
2012
CO: 08 0
NOz NOz
08: : a
_
TSP... .:TSP. ... .. 0.26 . -04 95 AFTER
PM10 PM10 5. 0.26 : 04 95 AFTER
PM2. . . AFTER
:.0:26 .:04• � : 95:... •.
S02 .S02 OS 0. . ...:
:::: 0
HAP/TAP CAS Emissions Emission
Control
s Pollutants (In ` HAP/TAPS Estimation Emission
Efficiency � EF Control''
(see instructions) Method Code Y Factor
f Alphabetical: " ' Pounds/Year
p _ ) ( .-.,). : ;(Net after all controls)
- See Instructions .
2012
r 'I
sw
, y
:.:.
3Z: :.

Moncure Plywood LLC:.:
.:.
Emission'Source:::: : Sander.System
Source ID Number: ES-04; CD.-05
missionPoint: EP-05
' I
2012 Actual Process Throughput:
i
Sander.Operation Production 45;326,00.0.sf/yr
Emissions Summary:
Pollutant: Eiriisgion:Factor :Reference ::Emissions
M.: 1.15E-05 lb/sf .. .. .: �El
0.26 y
M-10 1.15E=051b/sf ::: 0:2fi::::: y
M-2.5 : I:15E-05 lb/sf I 026
References:
1. Stack Testing Data, 1995
. ..
+
.
a
d
_. ..
_... .

As entered in AERO
Facility Name: Moncure Plywood, LLC 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 2012
1. Emission Source ID (from permit)or ES-11
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 2012: 20625 TON/yr
(e.g. production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content 17
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 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 ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x
W)
(in 0.1 feet)
e 11.1 DOWNWARD—FACING VENT 70 1.25 72 0.45 33.13 silo vent
e ] 1.2 DOWNWARD—FACING VENT 70 1.25 72 0.45 33.13 silo vent
ep 11.3 DOWNWARD—FACING VENT 70 1.25 72 0.45 33.13 silo vent
e ] 1.4 DOWNWARD—FACING VENT 70 1.25 72 0.45 33.13 silo vent
27

Operating;Scenario: OS-,16 ..: Emissiop.Source/Group IDs.ES=11
•
10,Operating Schedule' (Source/Operating:Scenario that best characterizes Calendar Year 2012).
Hours per:Da 24 Days per Week 7 Weeks' er Year .- 52
.Y ( ) Y P. ( ): . : P ( )
.. .11:.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasona[Periods Percent:Annual Throu kh ut::
::..:
an=Feb +Dec arch—Ma une—Aug. ° Sept.-Nov: ° ..
sm
25% y. 25% .... : 012. 25/° 012 25/°
012 012 ... :: :-
h .13: Actual Emissions P er Pollutant Listed
Attac. :ca cu ations and documentation of emission':factors or other estimation.methods used.
r
Ein E C.. t 1GHG .. ... .
issions— mission on ro
Pollutants: CAS GHG: Estimation .. Efficiency Emission
Pollutants . . Method Code
(Net after Factor Ef Control
Tons/Year See Instructions all controls
. 2012
Criteria. Emissions— Emission Control
Pollutant :: Criteria.. ::: : Estimation... Efficiency Emission
(NAAQS) ... Ef Control
Pollutants
Code Pollutants Method Code (Net after Factor
(Tons/Year) (See Instructions) all:controls)
. ...... . ......
2012-
CO CO: 08
iNOx NOz
:08:
TSP..
TSP ... .. 0.02 . _. . 08 .. . 0.00167
i n P•M10 PM:10 0.02 08 : 4.00167
PM2.5.... ::::: PM2.5 0.02 :08 0.00167::::.
S02 0$ ...:
VOC VOC::: :. 08
Emission ..: ...:
HAP/TAP CAS Emissions Control
::.
Estimation : Emission
Pollutants (In HAP/TAPS Efficiency." EF Control
(see mstruchons) is I Method Code . Factor
Alphabetical:Order) (Pounds/Year) :: :. (Net after all controls) ;
See Instructions
:2012
i
11
� `a

- Moncure Plywood LLC . . : :.'
Emission Soutee: : Hog Fuel Storage Silo
h Source ID Number: IES-GWS (ES-11)
Emission point: EP-11
�l
_.
a 2012.Actual Process Throughput:
r
Hog Fuel 20,625 ton/yr
missions:Summary:
Compound Emission Factor Reference :: = Emissions
C M : 1.67E=03 lb/ton 1 0:017 ton/yr
M10: 1.67E-03 lb/ton .. ::::' 1 0.017 ton/yr... :::
1VI2.5
. 1,,67E-03 lb/ton _ . 1 ..:0.017 ton/yr
References:
1. U.S.EPA;'OAQPS, Compilation of Air Pollutant Emission Factors,AP-42;:Volume I:
Stationary Point-and Area Sources,Fifth Edition,Section 13.2.4,January.1995: Average
_l "wind:speed estimated.using average annual wind'speed for Raleigh,North Carolina listed
in Table 7:1-9.of AP-42'.
M Emission Factor,(ib PM/ton)=k*(0.0032):*(U/5)�'3/(M/2)14
k particle size.multiplier= .1.00
1 U=mean:wi speed= 7.8 mph ...: .
M=moisture content= 4.8 %
b ... . .
_p
..
.
.. . .

As entered in AERO
Facility Name: Moncure Plywood,LLC 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 2012
1. Emission Source ID(from permit)or ES12
Emission Source Group ID
2. Emission Source Description: dry wood residual storage silo that receives material from the dry wood residual
system cyclone ES03
3. Operating Scenario ID/Description: OS— 17/dry wood residual storage silo
4. SCC Number/Description: 30700799/Plywood Operations ;Other Not Classified
5. Throughput/units in 2012: 117533000 FT2/yr
(e.g.production or fuel use):
6. Fuel Information (if fuel is used) % Sulfur % Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-5 CD21 Cartridge filter(1,800 square feet of filter area
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
e —12 1VERTICAL STACK 60 0.7 72 0.45 13.57 silo erp
33

Operating:Scenario: OS=.1.7 Emission.Source/Group IDi ES 12-
10.,Operating Schedule: (Source/Operating:Scenario that best characterizes:Calendar Year 2012) ..
Hours per.Da 24 Pays per Week 7 Weeksper Year:, 52.
L_r .: .11.Typical Start&End Times For Operating Scenario: Start: 0' End: 2359
12. Seasonal Periods Percent:Annual Throu "h utc
Y
2 � Spt.. Nov.auFeb -+Dec 7 arch—May une—Au
25/ 25/ g. 25o1
F .
012 012. .. ... .
:
012
' 13: Actual Emissions per Pollutant lasted
Attach calculations and documentation of emission.factors or other estimation methods used: w.
Emissions— Emission Control..
.. .
GHG GHG 'Estimation Efficiency .:::Emission
CAS::: :. :: :.. . . .. .: Ef Control
Pollutants: Pollutants (Net after Method Code Factor
Tons/Year See Instructions), all controls
2012
!_ Emissions— Emission Control
Criteria Pollutant: : Criteria - : Estimation Efficiency Emission
(NAAQS) .:, 1 . .... : Ef Control
=h Code:. . Pollutants Method Code (Net after Factor ,, .
Pollutants
G. (Tons/Year) (See Instructions) all:coritrols)
2012
G ... .
CO CO: 08 _ : .: 0
. .: NOx
08:
x 0::. ::
TSP.. TSP ... .. .0.55 . 10 ...: ,
09:9
PM10 PM10::: . 0.55 10 99.9
Asa PM2.5 PM2.5. . .0.55 ::10 99:9::
S02 .
NO . .: VOC ::":. 08 0
RAP/TAP .. - CAS Emissions Emission
n
.. l
Pollutants (In'' HAP/TAPS Estimation E Emission
Contro
Efficiency EF Control
(see instructions) Method Code Y Factor
Alphabetical:Order) :. (Pounds/Year) : : (Net after all controls) ; ;(See Instructions)
nstructiotiS
... ::201.2
w as
I
: :.. ..
... .
34

1
Moncure Plywood LLC;
Emission Source::: . : Dry Waste System Dry Waste Storage:Silo;
:Source ID Number: ES-12, CD-21
Emission Point: EP-06,EP-12
i
2012.Actual Process Throughput:
Plywood Production 117,533,000 sf/yr
missions:Summary-
Pollutant
Emission Factor Reference Emissions
PM 9.29E-06 Ib7sf: q ::0 55 y
MV 10 9.29E-06Ib/sf77-
1 :.::: 0.55 t y. .::.:.
M-2.5 : : 929E-061b/sf 1 : : 0.55 tpy
r
References:.
1. Emission factor from original.Title V Permit Application
as
.
_ �

As entered in AERO
Facility Name: Moncure Plywood,LLC 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 2012
1. Emission Source ID(from permit)or ESl3—GMO
Emission Source Group ID
2. Emission Source Description: glue mixing, application and hot press operations, including curtain coater,
plywood spreader,25 press and 40 press and paper overlay operation
3. Operating Scenario ID/Description: OS— 10/glue mixing,application and hot presses operations(Hardwood)
4. SCC Number/Description: 30700780/Plywood Operations ;Plywood Press: Phenol—formaldehyde Resin
5. Throughput/units in 2012: 71248000 FT2/yr
(e.g. production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
FUGITIVE('NO erp for gluing and
erp-13 STACK 3.05 l 25 Area= press operations
35

y
Operating:Scenario: OS= 1 Emission Source/Group ID .ES 13=CrM0
+- 10;,Operating Sphedule: (Source/Operating:Scenario that best characterizes:Calendar Year 2012)
Hours per Day 24 Pays 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 :utc .
an-:-Feb +Dec o each—May o une-Aug., a Sept.-Nov. o. .:
2S/o 25/0 25/0. 25/0
012...'::: :: - - 012. 012
12 ... .
1�( -13: Actual Emissions-per Pollutant Listed': .
1 . Attach:calculations and documentation of emission:factors or other estimation methods used:
Emissions— Emission Control'
GHG CAS GHG Estimation.I.: 'Efficiency : Emission
I. Ef Control
'Pollutants Pollutants - . Method Code (Net after Factor
Tons/Year See Instructions all controls
..2012
k Emissions— Emission
Control.. Criteria ..
Pollutant Criteria .. Estimation::: Efficiency mission
Ef Control
Pollutants Code..: Pollutants Method Code (Net after Factor
:=: :(Tgps/Year) (See Instructions) all controls):
.2012... ..
: O ' CO, .: Og .
:
��.. . . NOz �::.�. NOg
TSP - . . ...: TSP.
1,84... .. 08 ...0.0000517. . .
PM10 PMIO 1 84: 08 0.0000517
.::. : PM2:5 . PM2.5 0.96 ::08 0.000027..:
S02 S02 '08:
a 'VOC: HOC .: 6.:82 08 0:0001915
HAP/TAP . : : : CAS ::-::Emissions
Emission Control
Estimation Efficient Emission
:Pollutants (In -. . - . HAP/TAPS �'
'(see instructions) Method Code:: (Net.after all Factor EF Control
Alphabetical'Order) ,: (Pounds/Year) )
See Instructions controls
2012
Formaldehyde:: . .:.: 50-00-0 334.8656 08: - 0.0000047
Methanol 67-56-1: 2279;936 08 -::: 0.000032
Methyl isobutyl:::-
108-10-1 ::: : 406.1136 08: 0.000:0057
ketone
— ' Phenol 108-95:-2. 783328 :: 08 :: ... ::::0.000011 ...
.. . . .
f
3:

As entered in AERO
Facility Name: Moncure Plywood,LLC 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 2012
1. Emission Source ID (from permit)or ES 13—GMO
Emission Source Group ID
2. Emission Source Description: glue mixing,application and hot press operations,including curtain coater,
plywood spreader,25 press and 40 press and paper overlay operation
3. Operating Scenario ID/Description: OS—28/glue mixing,application and hot presses operations,(softwood)
4. SCC Number/Description: 30700799/Plywood Operations ;Other Not Classified
5. Throughput/units in 2012: 46285000 FT2/yr
(e.g. production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
S. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpen-nit)
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 Vie
in 0.1 feet)
FUGITIVE(NO 2_ Terp for gluing and
erp-13 STACK 3.05 1_� Area= press operations
37

Operating Scenario: OS=28. . Emission Source/Group ID:.ES1:3' GMO
10:.0 eratin Schedule: (Source/Operating:Scenario that best characterizes.Calendar Year 2012.
P g ) : :: ... ... .
.... . .... .
Hours per,Da 24- Days per Week- 7 Weeks'per Year... 52.
mor ... .
11.,Typical Start&End Times For Operating Scenario: Start: 0 : .End: 2359 -
12. Seasonal-Periods Percent Annual Throu h ut:
... : ... : . �012
e t.. Yov.25% une—Au . 25/ 1
2512 012 ::: 012.anFeb +Dec ach—May
0 °d %
(� 13..:Actual Emissions-per PollutantUited;: .
Attach calculations and documentation of emission:factors or other estimation.methods used:
Emissions— Emission Control
h
t GHG GHG .; Estimation :.. 'Efficiency : Emission
CAS Ef Control
Pollutants Pollutants Method Code (Net after Factor
r' Tons/Year) (See:Instructions all controls
2012
am
Criteria
Emissions— Emission Control::
Estimation:::: : Efficiency Emission
Pollutant Criteria:�: '
:(NAAQS) EfControl
Code., Pollutants - Method Code (Net after Factor
Pollutants (Tons/Year) .(See;Instructions) all controls)
. 2012.
CO .: CO 08
NOg NOz ..: .. ::.'08
TSP TSP
..:1.2
. . 08: 0,0000517. ... ..
::::,JM10: ;P1YI10 .- L2: 08 0:0000517
PM2:5. PM2:5..: 0.62 . . ... :. . 08 0.00002T-
S02 S02 08:
VOC. VOC 5:62::: :,` 08 0.000243
HAP/TAP CAS .::::Emissions Emission
Control
ns Emission "
Estimation Efficienc
Pollutants (In HAP/TAPS Y 1
(see instructions) Method Code (Net after all Factor EF Control
Alphabetical Order) Wounds/Year) .'
See Instructions controls)
2012
...Acetaldehyde . . ...: 75-07-0 " 1.94.397 08: 0.0000042. . .
= Formaldehyde 50.-00-0.: 87.9415: 08 :; : 0:0000019
Methanol 67-56=1 ::-::6479.9 :: . 08 0.'00014: :
Meth 1 ethyl ketone :78-93-3 40.26795 08: 8.7E 7
Met lsobutyl _.
108-10=4 32.86235 08 '7.1E-7
etone .
Phenol 408-95-2 :_ 64.799 ::: : 08 0.0000014

L
k
.
I Moncure Ply
,wood LLC
Emission Source(s): Glue Operations and Pressing
Source ID Number(s)r ::ES-13
Emission Point: EP-13
2012 Actual Process Throughput:
`? Tom'IHardwood_Production 71,248,000.sf%yr,
I Total Softwood Production 46,285;000:sf/yr
Hardwood::`i ::: ': Softwood Total
't Compound. Emission f Emissions . Emission Emissions Emissions
Units. Ref. Units::::.Ref.
p t :Factor ton/. Factor ton/ :::ton/
yr
PM..:
5.17E-05 Ib/sf 1 ... .. .1:84 25.17E-05 Ib/sf 1: ...1.20 3:04
PM 10 : ': 5:17E=05.: lb/sf :::1 :' .1.84 5.17E=05 .ab/sf 1 A: : :1:.20: 3.04 =;
� A � M2.5 . . . 2.70E-05 = . lb%sf.. 1 1 '. 0.96.., . .2.70E-05 - lb/sf... 1. 0.62 1.59
OC: 1.92E-04 .::lb/sf I 1 1 6:82': j 2.43E-04 lb/sf: 1: 5.62 12.44
Emission Emissions Erriission Emissions Total
Compound. Units., Ref. Units Ref. Emissions
Factor Factor
: .:. .... . lb/ lb/
yr
r`} Acetaldehyde.. --... .. 2.... .. 4.20E-06 lb/sf 2 - 194.40 194.40
Formaldehyde:, .. 4.70E-06 .: lb/sf `::2: 334.87 1:90E=06 -ab/sf 2 87:94: 422.81
Methanol 3.20E 05 Ib/sf.. 2 2279.94. 1.40E=04 lb/sf,. 2 6,479:90 8,759:84
edi I Eth 1 Ketone::'::: -- 2 .8.70E-07 Ili/sf' 2: 40.27• 40.27
k
Meth`1.Isobu 1 Ketone � 5.70E-06 . lb/sf 2 7.10E"07 lb/sf 2 32:86 . 438.98
Phenol::::': 110)r05 .: .lb/sf 2 783.73 1:401r06 ,:lb/sf 2 64:80: 848.53:::
( References:
1. AP-42,.Section..10.5 Plywood Manufacturing,Detailed Data Tables,-January 2002;test data for Unit 1P176;press.most
similar to Mb cure Plywood.The AP-42 factor is based on:2 tests on two very different'presses.The test selected is the press
.that has throughput,.flow rate,,and product most similar to Moncure Plywood:;The other test was on:a,press with'Iow production:
gate,low flow rate,making thick board. PM10 rs assumed to equal PM,and PM2.5 is assumed to equal condensable PM:
LJ VOC factor is higher test value for THC:as.Carbon,converted-to propane,adding formaldehyde and half of methanol..
2. AP-42,Section 10:5,Table 10.5-6;Jan 2002. signifies:below test method detection limit:
i

As entered in AERO
Facility Name: Moncure Plywood,LLC 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 2012
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 2012: 35600 TON/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) % 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-12 CD18 Cyclone 60 inches in diameter
2 CS-12 CD03-WWTC Woodwaste transfer cyclone 154 inches in diameter
3 CS-12 C1306 Ba filter 7,095 square feet of filter area
9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
erp for dry waste
erp-08 VERTICAL STACK 51 3.5 80 55 31749.72 transfer cyclone and
ba filter
25

Operating Scenario: OS-20... Emission Source/Group IDs.G-27
10..0 eratin Schedule: Source/O eratin Scenario that best characterizes-Calendar Year 2012)P g .... . .. P. : g:
Hours per.Day 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 u:tC ::... :...
25/
. 25%. Se t.-Nov.
012... :
25%-Feb +Dec a ch—May June—Au'
25/an
012 . 12012
13:_Actual Emissions er Pollutant Listed:
Attach:oalculations and documentation of emission:factors or other estimation methods used:
r�
Emissions— Emission Control
GHG
GHG Estimation .: ::: Efficiency Emission
CAS:: EfControl
Pollutants: Pollutants: Method Code : (Net after Factor
....:: hs/Yeaz See Instructions all controls
2012
Criteria . missions— Emission Control
. . ....
Pollutant:: Criteria.. : Estimation. . : : :: Efficiency :Emission
(NAAQS): .... . .. Ef:Control
Code:. Pollutants Method Code et after Factor
.Pollutants � �
Tons/Year) (See Instructions) all controls)
2012.
r CO. CO 08 0
NOx NOx 0$ 0.
TSP TSP 0.47 02 99:7 AFTER
PM10 .: PM1:0: 0.47 02 99.7 AFTER
PM2.5 PM2.5 .0.47 02: 99,7:. AFTER
S02 S02 : :08
VOC. VOC::: :: 08 .: 0
HAP/TAP CAS Emissions Emission .
• Control
I. Estimation Emission
Pollutants (In HAP/TAPS Efficiency EF Control'
i (see instructions) Method Code .: Factor
p ) ( ) (Net after all controls)
ca:Order) ::: : Pounds/Year : :L a eti See Instructions
2012
.. ..

i
Moncure Plywood LLC: .
Emission Source:: 'Green Chip Sizing,.Rechip,-:Transfer
'
Source ID Number: .... ES-17,ES-18,ES-14
Emission Point: EP-14
2011Actual Process Throu h ut:
-t .g.P . •
Tons Green Chips 35,600, ton/year:
Emissions.Summary: w.
"
Pollutant Emission Factor Reference Emissions
W 530E-02 lb%DT 1 : 0.47 t y
::... P1V1'10 5.30E-OZ. lb/DT 1 0.4.7:: 'y '
PM-2.5 : : 5.30E=02 1b/DT 1 0.47. .
r y..:
r .
References:.
1. Weyerhaeuser Test Data,Title:V Bulletin#19
_.
pw
w.
f�} ... ...... ,... .... ..
L.J ...: ...: .... ....
b.
__ .... ..

As entered in AERO
Facility Name: Moncure Plywood,LLC 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 2012
1. Emission Source ID(from permit)or ES16
Emission Source Group ID
2. Emission Source Description: Plywood waste hog
3. Operating Scenario ID/Description: OS—9/plywood hog
4. SCC Number/Description: 30700710/Plywood Operations ; Sawing
5. Throughputtunits in 2012: 3640 TON/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-3 CD03—WWTC Woodwaste transfer cyclone 154 inches in diameter
2 CS-3 CD06 Ba filter(7,095 square feet of filter area
9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
erp for dry waste
erp-08 VERTICAL STACK 51 3.5 80 55 31749.72 transfer cyclone and
ba filter
41

Operating;Scenario: OS 9:: :. Emission>ource/Group IDc ES16,
10..0 eratin Schedule: Source/O erathi Scenario that best characterizes:Calendar Year 2012 p g .... . ( P. : g: )
Hours er_Da 24._ Da s er Week 7 W.eeks' er Year.. 52
:. . Y ) y: p (. �: . : p (. . )
i . .. . .. _ . ..
11.Typical ical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal.Periods Percent Annual Throu h put::
an=Fb +D;ec o/ t:rch—Ma... :y une=Au , t.=Nov
0 250 25/ g. ?5/ 25/ .:
12 2 ! < : 012.. 012
-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:contiols
LJ. ... ..
.... 2012
Emissions— Emission
Criteria . Cont. . ....
(NAAQS): Pollutant: Criteria.. ::: : Estimation Efficiency Emission
Ef
Pollutants Code:'''. Pollutants . . ..Method Code (Net after Factor Control
:
(Tons/Year) e.Iiistructions) all contiofs)
2012.
CO. .. .. :: 08 0
NOx NOz w.
:08 0::::: wr
TSP TSP 0..1: 02 -..: 59:9 0.053 AFTER
PM10 .: PM10: 0.1 02 99.9 0.053 :AFTER
PM2:5.... : . :PM2.5. . ::-.0.1 :02: 0::::: 0.053 .::::: AFTER,:
S02 S02 08
or w
I VOC: VOC 08 0
HAP/TAP CAS Emissions E ...... n Control
Pollutants (In IIAP/TAPS Estimation Emission
Efficient .- EF Control
j (see instructions) Method Code y Factor
Alphabet calbrder) (Pounds/Year)::: ;(Net after all controls)
See Instructions
.:::2012
L,
•
I
.. . 4

Moncure Plywood LLC:.
:Emission,Source::: . Plywood Waste Hog'
:
:Source ID Number.: ES-16
mission omt: EP-16
2011 Actual Process Throu g. P h ut
_. .
Tons Dry Wood 3,640 ton/year
Emissions Summary:
_ . .
-F-.
Pollutant: Emission Factor Reference :Emissions
: . .. .: M.: 530E-02 lb%DT. .. 1 .. .. .: 0.10 a y
PM-10 5.30E=02 lb/DT 1 O.10 a
M-2.5 : 5.30E=02 Ib/DT 1 0:10
_ Y
References:
1. Weyerhaeuser Test Data,Title V Bulletin#19
L J
.. .. . . .
... ... ..
L
. . ..
w.

As entered in AERO
Facility Name: Moncure Plywood,LLC 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 2012
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 2012: 28 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) gate(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
65

Operating Scenario: OS- I I r Emission Source/Group ID:.IES 19
0.0perating Seltedule: (Source/Oper:ating:Scenario that best characterizes Calendar Year 2012)
Hours per;Day ( 1 ) Days per Week ( 1 ) Weeks per Year (.44 )
.. .11.Typical Start&.End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h :utc
an-Feb +Dec arch—Ma une—Au . Se t.-Nov.
25% Y . 25% g )5% p 25%
012 012 .. : 012 2
13, Actual.Emissions per Pollutant Listed
Attach calculations and documentation of emission:factors or other estimation methods used:
w Emissions- Emission Control
GHG q GHG Estimation Efficiency Emission
CAS Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions :all controls
2012 . .
Criteria Emissions- Emission Control
Pollutant . . :: Criteria Estimation Efficiency Emission
fNAAQS)Pollutants
Ef Control
Code Pollutants ., Method Code .(Net after Factor
(Tons/I'.eat) (See Instructions) all controls) "
2012
CO w CO 0101 68 0.95
NOX:: :: ...NOx 0.06. ::. :: 08
TSP :
TSP. .: .0 .08.. 0.31
j PM10 PM10 .:0 :"08 0.31
PM2;5:: P.M2:5 0. 08 0.3:1:
2... 0 08 0:29. ....:
VOC
VOC :. ::. :: .,0 08:: 0.35
Emissions: ; Emission Control
HAP/TAP CAS HAP Estimation Efficient Emission
Pollutants (In Alphabetical Order);: .(see instructions) Method:Code (Net after all. : Factor of
HAP/TAP
:.: :. {Pounds/Year .
. . . .:. EF Control
Se bstructions controls)
Acetaldehyde . _ 75­07-0 , .., 0.02148 08.. ". , 0.000767 ... ..
Acrolein 107-02-8 :: 0.00259 08 0.0000925
Benzene,: :71.-43-2 0.0261 Z:,::: 08 0:00.0933
Benzo(a)pyrene(Com f
ponent o
.. 50 32=8 0.00001 O8 : .1.88E-7
POMTV POM7 : .: ...
:
Formaldeh .de. .50-00-0. 0:03304... .. 08
i Naphthalene(Component of
POMT 91=20 3 0.00237 08. 0.0000848 .
- Polycyclic Organic Matter-(Inc
PAH,dioxins,etc:NC.AP 42 P.01VI 0.0047::. :: 08 0:000168 .:
historic,amor hous glob),.
. . ......
Toluene 108-88-3 0.01145 08 0.000409
X Ilene::: 1330-20-7 0.00798::::: 08 0-'000285
:66 .

i
,i—
Moncure Plywood LLC:
Emission.Source•::.. : 250 HP Diesel-Mred'Water Pump
Source ID Number: ..:: ES-19
yy 2012 Ae' fiW Process:Throughput:
:-Hours ours o peration 44:Hr/yr
No:2 Fuel:Oil Usage205. . .... . .. . g aU Yr ..
Heat Ii pui(250 hp) 28:0 MMBtu/yr::
j Compound, Emission Factor Units,_ Reference ssions.:
ton/yr
C.O.. 9..50E-01 lb/T&MRu . ... ..1 0.0.13.
Ox .: ,4.41E+00 lb/M1VIBtuO:0617
M - 3.10E-01 -Ib/M1VIBtu. 1... 0.004 .,
PM10 3a0E=01 lb/NIIVIBfu 1 0.004
_..
;M2.5 3.10E-01 lb/NBMtu 1 0.004
S02 2.90E-01 lb/1VINIBtu 1 4:06E-03 :
OC 3,50E-01 lb/M1YIBtu ',. 1 .4.90E-03
Compound Emission Factor: : Units Reference
Errussions.
lb/ .
I
Acetaldehyde(TIT) -7:67E-04 lb/1VIlv1Btu 1 . 0.0215
crolein(TH) 9.25E-05 lb/ZvMtu 1 0 0026
enzene(TH) 9..33E-04 lb/MMBtu 1 01026
--, enzo(a) yrene. (T) 1.89E-07'. lb/M1VIBtu 1 :: 0.000005
ormaldel yde.(TH). 1..18E-03.: lb71V11VIBtu.: 1 ,..; 0:033' .
- Naphthalene (H) 8.48E-05 lb/N MBtu
Toluene(TH): .: .4.09E-04. lb/MNIBtu 1..: . 0.0,11
ylene(TH) 2..85E=04.: lb/MNIBtu 1 0.008
rr
OM 1.68E 04' lb/NIl��Btd... 1 . 0.005: .
References: ::...
1 -AP-4 ,Section 3.3,Table 3.3-1
i

.ti.
As entered in AERO
Facility Name: Moncure Plywood,LLC 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 2012
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. Throughputtunits in 2012: 117533000 FT2/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) ro
Sulfur /o Ash Heat Content 17
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)
LRP_20 FUGITIVE(NO 1 100 Area= 1 Vats
STACK
43

l :.
Operating Scenario: OS - 18 : Emission Spgrce/Group ID ES20.
10.':Operating Schedule: (Source/Operating:Scenario that best characterizes Calendar Year 2012) :
Hours per:Day ( 24- ) . Days per Week (.7 ) . .Weeks per Year, {.52. )
L_J :: .11. Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h :ut:
an=Feb +Dec arch-Ma une-Au' .. S,e t.-Nov.
2S% 6 . Y 25% . g 25% p 25%
012 012... ::: :: 012. 012 :.:.
13. Actual Emissions er Pollutant Listed s .
Attach:calculations and documentation of emission:factors or other estimation methods used:
Emissions- Pmission, Cont :.l
missions � . Control
GHG GHG ::.:: Estimation Efficiency .::'Emission t I
CAS ::
Ef Con ro
Pollutants Pollutants. . Method Code:'. ... (Net after Factor
::Mns/Year) (See:Instructions all controls
2612
Emissions- Emission Control. ... ..
Pollutant Criteria :: :: Estimation. ::: :: Efficiency Emission
(NAAQS) Ef:Control
Code. Pollutants Method Code. .
. Pollutants (Net after Fac
tor...
,
(Tons/Year) (See;Inkiuctions) all:controls).:
2012 ... ..
CO CO.. 08
NOx NOa _,. ::08
TSP TSP :. 08..:
! :::PMI0.: PM10 08 _. ..
08 _..
S02 S02 08...:
VOC VOC 2.15 08
HAP/TAP , Emissions
Emission Control
CAS Estimation Effic enc Emission ""
.Pollutants (In HAP/TAPS Y. l
P .. (see instructions) . _ Method Code.'. . (Net after all' Factor
Alphabetical Order) (Pounds/I'ear): ..
EF.Contro
See Instructions controls)
2012
,Acetaldeh de .75-07-0 .552..4051 08- m = 0,0000047
-' Methanol 67-56-1 857.9909 08 00006073
.-
..
.
.. . .
:
44::..

J.
Moncure Plywood LLC::: .:
Emission Sources : : Vat Operations
s Source ID Nurriber(s):: ES 20.
Emission=Point: EP-20
2012 Actual Process Throughput:
Total ar :wooProduction 71,248,000 sf/yr
�. ... . ,..... Total Softwood Production 46,285,000 sf/yr ::
Emissions
Compound Emission'Factor Units Reference
.ton/ r.. ..
�i VOC-Hardwood 1.20E-05 Ib/sf 1 0.43
VOC-'Softwood 7.44E-05 lb/sf 2. 1.72
Totai VOC
2.15
`- Emissions ...:
Compound Emission Factor Units: Reference
:. :.
lb/yr
Acetaldehyde. . ...: 4.70E-06 'Ib/sf 3. 552.41.. ..
,. ... .. IMethin6l 7.30E-06.:: ::: :: lb/sf :::, 3 857.:99..
References:: . : .
L.'AP-42 Section 10.5,Table 10.5-7,Softwood plywood log vat,.Sum:of:VOC compounds
excludin menes.
2. AP-42 Section 10.5;Table 10.5-7;-So#twQad 1 wood to vat,Sum of VOC com ourids.
i . p Y. .. g p
.. . including pinenes.
_.. .
3. AP-42 Section.10.5,Table 10.5-7
S
1 h ..

As entered in AERO
Facility Name: Moncure Plywood,LLC 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 2012
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. Throughputlunits in 2012: 3300 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 inpen-nit)
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(Aefm)
Rectangle(L x Vie
in 0.1 feet)
EP-21 VERTICAL STACK 20 1 70 10 471.23 End Sealer Spray
Booth
45

{
Operating cenarro: OS-33 Emission.Source/Group ID:.ES21
10..Operatin2 Schedule: (Source/Operating Scenario that.hest characterizes:Calendar Year 2012).
Hours per..Day (-24 ') Days per Week - ( :7 ) . .Weeks per Year (.52.)
w.
- la.,Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut '
.. ..
v
une-Aug. 25/ Sept.:Nov.25/ 25/012an=Feb +Dec 2o rch-May
012 / 012
!' 13: Actual Emissions er Pollutant Listed p p
_. Attach calculations and documentation of emissiori:factors or other estirriat on methods used. -
- Emission Control
Emissions "
GHG . ..
GHG .:::.:� Estimation .::'. . Efficiency .:::Emission
CAS :: .: Ef:Control
Pollutants Pollutants (Net after Factor
Method Code.
.::. Tons/Year See:Instructions all controls
It
2012
: :'
Emissions- =Emission Control...
Criteria,
Pollutant Criteria: : ' Estimation. ::: :: Efficiency Emission
Co
} (N AQS) Ef:Control
Pollutants de. Pollutants Method Code. (Net after Factor
(Tons/Year) (See Instructions) all controls).,
2012 . ..
CO' .: CO.. .. 08
.
.' NOx NOx
TSP. .. 0109 03 TSP `. • ..
::PM10 .. PM 0.09 03 ;
PM2.5 : ::. PM2.5 . ..
"
48 ..
S02 .: S02
VOC .: VOC :: .: 0.05:: 03
Emission Control
HAP/TAP ....: Emissions . ...
CAS Estimation Efficient Emission "
Pollutants (In HAP/TAPS ..... Y: I
see instructions EF Control
. ... ..
h Alphabetical Order) ::: -. (Pounds/Year) Method Code:::.:: (Net after all Factor
See Instructions): controls)
2012
Yin l acetate 1.08-05-4 8.19 03 q.
--
q as
y
k
r
46

Moncure Plywood LLC:
Emission Source(s): End Sealer Spray Booth
Source ID Number.(s): ES-21:
Emission Point: EP-21
C _
2012 Actual Process_Throughput: -. ..
- End Seal Material Usage 3,300 gal/yr
S ra Booth Filter Efficiency.. 97.5%
Emissions
Compound Emission Factor Jnifs Ref
t r.on/ ..
. ..
1VI 90% : %wt :.. ..1 . 0:09.. ..
3' M10 90% %wt 1... 0.09. .
VOC:: 0.4% °lo wt 2 0.05
Compound Emission Factor Units Ref Emissions
Ab/vr
myl acetate..: 0.031% %wt.,.: 1 2,3 8.19_ ..
References:..:
.. . . .. . - .
1. Conservatively assume 90%solids in material.Assume 30%overspray into:filter.
2:.Compound speciationfrom MSDS,April 2010. .Specific gravity is:0:96.
3. Compound speciaiion from WVCO letter,April 26,2012.
1
-_j

As entered in AERO
Facility Name: Moncure Plywood, LLC 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 2012
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: Not required by facility,will be completed by DAQ
5. Throughput/units in 2012: 53000 FT2/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-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 ft (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
47

As entered in AERO
Facility Name: Moncure Plywood, LLC 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 2012
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 2012: 20625 TON/yr
(e.g. production or fuel use):
6. Fuel Information (lffuel 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 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 V)
in 0.1 feet)
FEP—FUG FUGITIVE(NO 1 72 Area— 1 ERP for Fugitive
STACK) sources
49

P g.
OS -2; Emission Source/Group ID: I.1:
10..Operating Schedule: (Source/O.perating:Scenario that best characterizes Calendar Year 2012-)
_ Hours per:Day ( 24 ) Days per Week (.7 ) . .Weeks per Year (.52 )
Ias q
1.1.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
YP P... g
12. Seasonal Periods Percent Annual Throu h ut:
o Y o g o P So/. :
an-Peb +.Dec arch—Ma une-Au . Se t.—Nov.
25/0 25/0 25/o 0
012 2
012... ::: :. 0:12. 012
13: Actual Emissions er PollutantListed
Attach:calculations and documentation of emission;factors or other estimation methods used:
emissions— Em ission Control
� : GHG
CAS:: :.
GHG Estimation Efficiency :::Emission
Pollutants Ef Control
Pollutants ,Method Code
(Net after Factor
r } -.Tons/Year See Instructions all controls '
2012
Emissions— Emission Control
Criteria
Pollutant:: Criteria Estimation .. : : : Efficiency Emission
(NAAQS) Ef Control
1 Code Pollutants Method Code (Net after Factor
Pollutants Tons/Year See Instructions) all,controls
2012 q.
CO. CO. .. . 08
NOx NOx
TSP. TSP ... .. . . 0:03 . 08 . .
.0.0.027
I F PMI0 PM10: 0.03 08 0.0027
PM2.5 PM2.5 :0.03
S02 S02
J ) ::VOC .: VOC :: .: 08
or HAP/TAP .. CAS ..Emissions Emission
Estimation Emission
Pollutants (In HAP/TAPS EF Control
ontrol
i: .� (see instructions) Method Code.: Efficiency Factor
J Alphabetical:Order) : : :- (Pounds/Year) .: - . . (Net after all controls) .
See Instructions
.... _.
.::'2012
_. .
w.
ps
I
i
50.

As entered in AERO
Facility Name: Moncure Plywood,LLC 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 2012
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 2012: 976 TON/yr
(e.g. production or fuel use):
6. Fuel Information (if fuel is used) /o Sulfur /o Ash Heat Content
(Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
i i i 1
9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
('in feet) Circle(enter#): (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
EP—FUG FUGITIVE(NO 1 72 Area— 1 ERP for Fugitive
STACK) sources
55

`, . . .
Operating Scenario: OS 3 Emission Source/Group ID: I-2.
to..:Operating Schedule; (Source/Operating:Scenario that best characterizes.Calendar Year 2012)
Hours per,D.ay '(24- Pays perWeekj.7 Weeks er-Year. 52
- 11.Typical Start&.End Times For Operating Scenario: Start: 0 End: 2359 ::
12. Seasonal Periods Percent Annual Throu h utf
9- an-Feb +.Dec arch-May o : une-Aug.. o Sept.-Nov. 50/
: . :25%0 25/o 012. 25/0 012012 0
.
13. Actu.l.Emissions per Pollutant Listed
l - Attach calculations and documentation of.emission:factors or other estimation methods used:
Emissions- Emission Control
GHG ::..: Estimation Efficiency Emission
Pollutants: CAS •
Pollutants . - Ef Control
Method Code (Net after Factor
Tons/Year See Instructions all controls
Lj 2012
f Criteria
Emissions- Emission Control...:
Pollutant:: Criteria Estimation...,: Efficiency Emission
_t (NQS): Ef Control
E
' Pollutants
Code'- . Pollutants Method'Cod6 (Net after Factor... ..
(Tons/Year) (See Instructions) all:controls) ..
2012
' CO CO: ..08
NOz .. �: NOz ..,. :08: :. ..
TSP. ...TSP.... ._ 0 08
r PM10. PM10 . .. 0 08
PM2.5 . PM2.5
S02 ..S02 0.8 ...:
VOC : VOC 08
HAP/TAP CAS Emissions Emissio'n Control
j Pollutants (In'` HAP/TAPS Estimation Emission
P Efficiency EF Control
i (see mstruct.ions) Method Code.. Y Factor
Al habetical:Order Pounds/Year :
1 P ) ( )' See Instructions ; (Net after all controls)
.::'2012
i r . ..
an a
lam` . . .. ... . . ...... . . .. . . . ..
::56

I
Moncure Plywood LLC:::
Emission Source::: . : Core Chipping
Source ID Number: IS-IN-2
Emission Point: IS=IN-2
.::: .
2012.Actual Process Throu h ut
Cores Chipped 976 ton/year
r •
:.: :..
Emissions:Summary:
Pollutant Emission Factor Reference :Emissions
M 2.70E-03 11blton 1 . 0.001
y ,
M40 I 2.70E-03 lb/ton 1 O.00:I:.
..:
References::. :
..1:. AR-42 Section.13.2.4
JJ
l._
r _
c
�`.

As entered in AERO
Facility Name: Moncure Plywood,LLC 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 2012
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 2012: 34624 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#): (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
57

Operating:Scenario: OS -4: Emission.Source/Group ID: I-3
O..Operating Schedule: (Source/Operating:Scenario that'6est characterizes;Calendar Year 2012)
Hours er.Da 24 Week 7
P.. Y Da.,s.per( ) Y P. ( ): . Weeks per Year ::(..52 )
.U..Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent:Annual Throu h ut::
{- an-Feb +.D.ec o o une-Aug. o Sept..Nov. 2 u/
012
: . .25 ' 25/0 25_/0 5 0
�arch-.May .
12:::: :: ::
11 Actual-Emissions per.Pollutant Listed.: -
Attach:calculations and documentation of emission factors or other estimation methods ethods used.:
sm
Emissions- Emission Control
GIiG aGHG-. . Estimation.,. : Efficiency Emission
Pollutants; CAS : Ef Control
Pollutants . . Method Code :(Net after Factor
... ..ons/Year See Instructions all controls
2012. ....
J. . ..Criteria .
-Emissions- Emission Control. .:
Pollutant :: Criteria:; Estimation... : : :: Efficiency . :::Emission
(NAAQS): Ef Control
Pollutants Code Pollutants Method:Code (Net after Factor ..
.. ... .. ....
(Tons/Year) {See:Iristructions) all:contcols)
2012
CO CO: 08
:. NOx :: :: NOx
TSP.. TSP ... .. 0.05 . 08
0.0027
PM10 PM10: 0.0.5 :: 08 :: 0.0027 -
PM2.5 :; PM2.5 .. :.05 08 ...... 0.0027
r-
.... S02 S02 08
::VOC r VOC.;. . 08
HAP/TAP ....Emissions
Emission
CAS Estimation Emission
Control
Pollutants (in HAP/TAPS.,
see instructions Efficiency EF Control
...
( ) Method Code .: Factor
Alphabet cal Order) (Pounds/Year): ': ... (Net after all controls)
See Instructions .
:::2012 .. .
4.
:.
58

rr
I�
Moncure Plywood LLC
Emission Source.,,:,:: Green.Veneer Hogging Operations
_ ..
Source ID Number: ...: IS IN-3
Emission'Point: IS -IN-3
2012 Actual, .Process Throughput:
Green Veneer Hogged. 34,624 ton/year.
missions: _ummary:
Pollutant: Eriisson Factor Reference : Emissions
PM.: 270E=03 lb%ton 1 0.05 t
y::
M-10 2.70E-03: lb/ton ;::1 0:05 toy . :.
PM-2.S : 2.70E-03 .. lb/ton 1..; 0,05 . .
f
References:
1. AP-42:Section 1:3.2.4
ii
or w
. . ... . . ....

As entered in AERO
Facility Name: Moncure Plywood,LLC 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 2012
1. Emission Source ID (from permit)or Group G-25 consisting of I-4, I-5
Emission Source Group ID
2. Emission Source Description: Ink and painting operations
3. Operating Scenario ID/Description: OS —5/lnk and painting operations
4. SCC Number/Description: 40500597/Printing—General ;Other Not Classified
5. Throughput/units in 2012: 1161 GAL/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
Device or Stack):
8. Control Device Information :None
Order CS-1D CD ID Control Device Description
as listed inpermit)
9. Emission Release Point EIR 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
23

I '
- Operating Scenario: OS-.5:: Emission Source/Group ID: G-25 _
ti •
10.:Operating Schedule: (Source/Operating:Scenario that best characterizes,Calendar Year 2012)
Hours per:Day ( 24 ) Days per Week ( 7 ): Weeks per Year .( 52 )
11. Typical Start&.End Times For Operating Scenario: Start: 0 :: End: 2359
12. Seasonal'Periods Percent:Annual Throu h ut
an-Feb .+Dec o arch-May o une-Aug.- o Sept.-Nov. o
25/o : 25/o Z5./o 25/o
012 :. : 012:::: :;: :. .: 012: 012
13. Actual.Emissions per Pollutant Listed
- Attach calculations and documentation of emission:factors or other estimation methods used.'
b.
i Emissions- Emission Control
GHG
GHG- : : Estimation. Efficiency :Emission
CAS: ... . .. . . Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See.Instructions all controls
2012.
... . ..
Emissions- Emission Control.
Criteria
Pollutant::: Criteria:: : Estimation_ Efficiency Emission
(N_ QS): Ef Control
Pollutants Code- Pollutants Method-Code (Net after Factor.
(Tons/Year) (See Instructions) all controls)
2012
:CO CO q 08
NOx
NOx
P. P ... .. 08
-, . ......
PMIO PM10: 08
PM2.5 :: PM2.5 .::08 ... .. .
S02 S02 08 .
:.VOC .. VOC:= 0.42::; . ."" 03 ..
HAP/TAP .: Emissions Emission
Control
CAS Estimation Emission
i Pollutants (In HAP/TAPS... . Efficiency EF.Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year): (Net after all controls)
.See Instructions .
2012
t .
24

Moncure Plywood LLC:::.
�
Emission Source:_:: ;:: Ink and O erations.. g p
Source ID Number: .. IS-IN-4,IS-IN-5
Emission Point: I84N-4 IS-IN-5;
2012 Actual Process Throughput:
Lo o aint usa e: 866
g .g gal/Yr
P
Inkusage
Ink density 295 :gaUyr.
.... . ..
8.21 Ib/gal
lJmissions Summaryt
Pollutant Emission Factor- Reference: Emissions
VOC=logo •aint 4.00E=01 lb VOC/ al
g g 1 0,17
— Y
VOC.-ink ' 2.00E-01 1b VOC/lb:. 1 ... : 0.24
Total VOC .. :. .
0.42 t
References:.. .. .
1:'Material Safety Data Sheets
... .. .. .
' .. .. ..
i

As entered in AERO
Facility Name: Moncure Plywood, LLC 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 2012
1. Emission Source ID(from permit)or 1-6
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 2012: 18810 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 inpen-nit)
�--1 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— I ERP for Fugitive
STACK) sources
59

Operating Scenario: OS -.6: Emission Source/Group ID: I=6
10.:0 eratin Schedule: Source/O: eratin :Scenario that best characterizes.Calendar Year 2012
Hours per;Day ( 24 ) Days per Week ( 7 ). :::Weeks per Year, ( :52 )
L :-.11.Typical Start_&:End Times For Operating Scenario: Start: 0 End: 2359
q.
12'. Seasonal Periods Percent Annual Throu h uti
- an—Feb +.Dec o h—May o une—Aug.. orept.—Nov._ o
25/0 25% _ 25,/ 77
0 25012 rarc.
12:::: 012: 12rw
13.'Actual.Emissions per Pollutant Listedw.
Attach calculations and documentation of emission factors or other estimation methods used:
:'Emissions— Emission Control
: GHG GHG.. : : Estimation... : Efficiency Emission
CAS :EfControl
Pollutants Pollutants . . .. Method Code . . .. (Net after Factor
w. . ... ..
Tons/Year See,Instructions all.controls
.2012.
Emissions— Emission Control
Criteria .
Pollutant:: Criteria..::::: Estimation. . : : Efficiency Emission
(NAAQS): Ef Control
C Pollutants' M e et after Fa
As Pollutants . Code: oll.utan Method.Cod (N Factor:: .
(Tons/Year) (See Instructions) all controls) .
2012
CO, CO 08
h ... .. .
NOx NOx 08:
TSP. TSP.-. :. 08
k .PM10 PM10;. :. 08
`I PM2.5 PM2.5 ::0.8
SO2 _SO2 .08.. .
..VOG VOC 2.97: 03 .. 0:316
:. HAP/TAP Emissions Emission Control
CAS Estimation Emission
! Pollutants .(In I�AP./TAPS.. Efficiency ' EF Control'
1 . (see instructions) Method Code.: Factor
�b Alphabetical Order) (Pounds/Year): (Net after all controls)
See Instructions:)':.
2012
L. ... ..
... .. .
::60

Moncure:Plywood LLC
Emission Source:::.., Plywood Surface Patching:
Source ID Number: . IS-IN-6
Emission Point: :: IS-IN-6
2012 Actual Process Throughput:
. .
Gallons:Used 18,810 gaVyr
Emissions:Summary:
:Pollutant: Emission Factor :Reference Emissions
VOC 3;16E-01 lbi al 1 2.97
g y
References:
1 Material Safety Data Sheet qps
w.
L '
L �:

As entered in AERO
Facility Name: Moncure Plywood,LLC 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 2012
1. Emission Source ID(from permit)or 1-7
Emission Source Group ID
2. Emission Source Description: Maintenance parts washers
3. Operating Scenario ID/Description: OS —7/Maintenance parts washer
4. SCC Number/Description: 40202105/Flatwood Products Coating;Equipment Cleanup
5. Throughput/units in 2012: 110 GAL/yr
(e.g.production or fuel use):
6. Fuel Information (1f fuel is used) /o Sulfur % Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
& 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—FUG FUGITIVE(NO 1 72 Area— 1 ERP for Fugitive
STACK) sources
61

Operating:Scenario: OS-7 :: :. Emission.Source/Group ID: 7: :
10...0 Operating Schedule: Source/O eratin Scenario that best characterizes Calendar Year 201.2
P g ( p g; .) ...
Hours perDay 24, Da s per Week 7 Weeks per Year:: 52
I Typical Start&:End Times For Operating Scenario: .::.Start: 0 End: 2359
Ii Seasonal:Periods Percent Annual Throu h ut:
+. .. — — —an—Feb Dec 0 arch May o une Aug. 0 �012
ept. Nov... .. 0
.. :25/0 25/o 25%0 25/o
01:2 012.:.. :: 012:
13. Actual-Emissions per Pollutant Listed': -
Attach calculations and documeritation 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
: ons/Yeaz) (See Instructions all controls
2012:
A Criteria Emissions— Emission Control..
Pollutant:: Criteria : ` Estimation Efficiency Emission
(NAAQS)` El Control
Pollutants Code Pollutants Method.Code (Net after Factor
(Tons/Year) (See:Instructions) all:controls) .
: .. 2012
CO` 08
NOz• NOx 08:'
T.SP. TSP,.,. .: 08
P1VI10 PM10. .. 0.8_
PM2.5 ... PM2.5 ....... 08..', . ...
S02 S02 08
VOC: 0.39 03
HAP/TAP CAS Emissions Emission Control
Pollutants (In HAP/TAPS. . . Est�mahon Emission`
(see instructions) Method Code , .: Efficiency Factor l
Alphabetical Order) (Pounds/Year): (Net after all controls)
EF.Contro
See Instructions).
. :2012
k1
LJ
we q
,_,:

"
oncure Plywood LLC::-
Emission Source::: :i Maintenance Parts Washer
Source ID Number: IS-IN=7
Emission Point: IS-IN-7
2012 Actual Process Throughput:
`1 Gallons:Used: 110 gaUyr
.
Emissions:Summary:
Eolliitant Emission Factor Reference Emissions
VOC ."I 7:GOE40 lb/gal 11 0.39
r _ .
References:
w Material Safety Data:Sheetqj
. . . . . .
a
. . ..
F. -
t
b
' .

As entered in AERO
Facility Name: Moncure Plywood,LLC 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 2012
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 2012: 185015 TON/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
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpen-nit)
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
63

17 ...
Operating:Scenario: OS-8 :: : Emission_Source/Group ID: 1-8
10., Operating Schedule: (Source/O:perating:Scenario that Best characterizes:Calendar Year 2012)
Hours er:Da 24' Days per Week"Weekj 7 Weeks " er Year.:: 52
J.-L Typical Start&:End Times For Operating Scenario.: . ::Start: 0 .::::End: 235§
j
12. Seasonal Periods Percent:Annual Throw h itt::
an—Feb .+.Dec o arch-May. o une—Aug. o Sept:—Nov., o
012 25/0 012 25/o . 25./0 25/o
:. : 012: . .. 012
11 Actual-Emissions p er Pollutant Listed
Attach cdlculations and documentation of emission:factors or other estimat ion methods used.:
4 : Emissions— Emission Control
GI3G: GAG .. :: Estimation. Efficiency Emission
: CAS Ef Control
Pollutants Pollutants Method Code (Net after Factor
Pollutants'
.
n • ... :T ns/Year) (See.Instnictions all controls)
J
... .. 2012. �.
�Em.issions—_., . Emission Control
-- Criteria: . : ..
Pollutant-:. Criteria:: : Estimation::: Efficiency Emission
(NAAQS): Ef Control
Pollutants
Code" Pollutants Method.C.ode" '(Net after Factor .. .
(Tons/Year) (See:Iiistructions) all.controls) .:
2012
CO. CO .: .. 08
NOx NOx 09 _ ..
TSP.. TSP ..: .. 2.45 02 ..
PM10 = PM10:: :. 2.45 02
4 PM2.5 : PM2:5 08
S02 S02..:.. .. 08
VOC VOC 08
HAP/TAP Emissions Emisston
' Control _
CAS Estimation Emission
Pollutants (In HAP/TAPS. : Efficiency EF Control
(see instructions) Method Code Factor
Alphahettcal Order) (Pounds/Year) (Net after all controls)
•See Instructions -
:.2012

Moncure Plywood LLC...
Emission Source:,: Veneer D verter Exhaust Cyclone
Source ID Number: IS-IN-8
Emission Point: ::•IS=IN-8
-� 2012 Actual Process Throughput:
. .
1 Wet wood. 185,015 'ton/y.
Emissions'Summary:
ummary:
Pollutant Emission Factor Reference Emissions
I 5.30E-02 lb/DT: : 1 2.45't y:`.
} M-10 ,:' . 5.30E-02 lb%DT :::: 1 2'.45
YReferences:
4
' 1. Weyerhaeuser Test Data,Title V.Bulletin#1'9
.::
sw
sm
1
_ .
.

As entered in AERO
Facility Name: Moncure Plywood,LLC 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 2012
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 2012: 117533000 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
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—Fu 4 FUGITIVE(NO 72 Area= 1 Stackers
g STACK
5

Operating:Scenario: OS 32: Emission
10.;Operating Schedule: (Source/O:perating Scenario that'Best characterizes:Calendar Year 2012)
r Hours per-Day 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 jhput:
an—Feb .+.Dec 1:- % a"rph..-MaY: o une—Aug. 20/ ept: Nov,, ., o2525/0 : 5 0" 25/0
012 012 012: 012
( 11 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/Yeaz See.InstrUctions all controls
2012.
Criteria Emissions— Emission Control
Pollutant:: Criteria Estimation:: Efficiency Emission
(NAAQS) Ef Control
Pollutants Code Pollutants Method.Code (Net after Factor ... .
_ . . .
:....
{Tons/Year) (See Instructions) alf controls) .
2012
r� CO CO ...... 08
NOz, NOz .08.
TSP., ..TSP...: 0:01 . 08.;
PM10 PM10 0.01. :: 08
PM2.5 :: :. PM2.5 08:
:.08 "
F VOC VOC 08
.HAP/TAP Emissions mission E
Control
Estimation Emission
Pollutants (In CAS HAP/TAPS . Efficiency EF.Control
(see instructions) Method Code :.Factor
Alphabetical Order) (Pounds/Year) (Net after all controls) . .
See Instructions)*•
2012
ss
6 .

�. .'' ::... Moncure PlY wood LLC
Emission Source:. Green Veneer'Stackers
'Source Source ID Number: IS-IN-9,IS-IN-10
Emission:Point. ISJN-99 IS-1N—40
2012 Actual Process Throughput.-
Total Plywood Production 117,533,000 sf/yr
-missions.Summary:
Pollutant Emission Factor ]::Reference Stackei.No:. 1 Stacker No:2
Emissions Emissions ..
M:_ :: ;.1.89E-07 lb/sf: .: 1 5.55E-03 tpy 5:55E-03 tpy
M=10 -1.89E-07.. lb/sf' 1 . 5:55E-03.tpy 5.55E-03..tpy
References:,
1:. Engineering Judgment
.....
-ti
Lj
pq
p:r so
y ti
.... .

As entered in AERO
Facility Name: Moncure Plywood,LLC 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 2012
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 2012: 4744 TON/vr
(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= I Hammer Hog Truck
STACK) Dump
51

Operating:Scenario: OS -.25: Emission.Source/Group ID:FI 11
10.:Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2012)
r ' Hours er:Da 24 Da' s er Week 7 Weeks er Year 52
perm Day ay 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 ° arch-May, o une—Aug. °/ . Sept=Nov... .. °
25/0 25/0 .
rp
012 012::.: : 012: 25 °.: 012 25/o
j ? 13. Actual-Emissions-per Pollutant Listed
.. . . .. . .
—' Attach calculations and documentation of emission:factors or other estimation methods used.
Emission Control
-::Emissions—
GHG GHG.. Estimation... : : :. Efficiency ::Emission
Pollutants CAS � : Method Code (Net after Factor Ef Control
Pollutants . . ..
...':Tons/Year See.Instructions all controls
2012.
_.
Emissions— Emission Control
Criteria: ... . . .
Pollutanti : Criteria:: : Estimation.: Efficiency :Emission
(NAAQS) � Ef Control
Pollutants
Code Pollutants Method.Code " (Net after Factor .. '
:::(Tons/Year) (See Instructions) all.controls) .:
2012
r CO CO: : 08
NOX..
z 08
TSP, ..TSP ... .. 0 08
7 . ...... , . ...... .
PM10 PM10: 0 08
P .:08:M2.5 PM2.5 S02 ..S02 .08 .. -
s YOC' .. VOC :: :. 08
Em
ission
HAP/TAP :: Emissions Control .:
CAS Estimation Emission
h Pollutants (In HAP/TAPS... . Efficiency EF.Control
(see instructions) Method Code Factor
Alphabetical Order) :'' '' (Pounds/Year) � .:: : (Net after all controls)
.See Instructions .
:2012
� :.
mw
o- .. .. ... .. ... .. ... .. ... .. ... .. . ... ..
52

Moncure Plywood LLC...
r Emission Source:.::::.: Hammer:Hog Truck Dump
'! Source ID Number: IS-IN-11. ..
Emission Point: IS-IN-11
is
2012 Actual Process Throughput:
Dry:waste 4,744 ton/yr :
Emissions:Summary:
1
Pollutant: Emis§ion Factor =Reference � Emissions
PM 1164E-05 IlbApn 1 3.89E-05 tpy
M-10 1 1.64&05: lb/ton , I 1 :3.89E-05
References::.:. :. .. :
L AP-42.Section 13.2.4
�y .. ..
.. .. ..

As entered in AERO
Facility Name: Moncure Plywood, LLC 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 2012
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 2012: 91 TON/yr
(e.g. production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur ro
Ash Heat Content
(Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpen-nit)
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—Fug2 FUGITIVE(NO 1 72 Area— 1 Dry Waste Truck
STACK) Dum
53

.. ..
Operating Scenario: OS-24 . Emission Sour ' Group ID'.1'11
t :. 10..;Operating Schedule; (Source/Operating;Scenario that best characterizes Calendar Year 2012)
. .
Hours per.D4y (24 ) Days perWeek (.7 Weeks er Year:, 52
L � U.:Typical Start&.End Times For Operating Scenario:. �.Start: 0� � � �.End: 23�59-
P:..: g ..
12. Seasonal Periods Percent Annual.Throu h :ut:
an Feb +Dec o arch—May ° une=Aug.. ., °� Sept..-Nov. °
012 :. :. ° 012.:. :.: :: ° 012,
25 °: 25/o
13. Actual Emissions per Pollutant Lasted
Attach calculations and,documentation of emission factors or other estimation methods used: :
:Emissions— Emission Control
GHQ GHG: Estimation Efficiency Emission
CAS: Ef Control
Pollutants: Pollutants Method Code (Net after Factor
r' .TofiYYear See Instructions all-controls
2012
Criteria ':Emissions— Emission Control.
Pollutant::' Criteria Estimation. Efficiency ::Emission
(NAAQS) . Ef Control
.: :Pollutants
Code Pollutants:. Method Code (Net after Factor
(Toris/Year) (See Instructions) all controls) .
.. . ..
CO CO 08,
i NOz NOg :'08
TSP TSP; 0 08 -.
PM'0 PM10 0 08
PM25 PM2.5' 08:
S02, 902
I I VOC VOC 08
.`: IAP/TAP Emissions
Emission Control
CAS Eshmation. Emission
Pollutants;(In HAP/TAPS Efficiency EF Control,
(see instructions) Method Code Factor
Alphabetical:Order) (Pounds/Year). S (Net after all controls)
'— •ee Instructions
.: :2012
ti ..
:: ; .

. .. ..
i .
Moncur 'Plywood LLC...:
Emission Source: Dry Waste Truck'Dum
Source ID Number:. IS-IN-12
' Emission:Point: ::: TS-IN-12
Z_
2012 Actual Process Throughput:
Dry waste: . 91 ton/yr.
Emissions:Summary:
Poilutant.: Emrission Factor :Reference- .:.Eriiissions
LJ. .
IVI 164E-05 ]b/t6n 1 :7.46E-07
Y :
M-10 :,: 1.64E-:05: Ib/ton 1 7.46E707=
- ,
References:::
L AP42 Section 13.2.4. . ..
..
�i
1q. _. .
,. or
..
a ... ... .. ... ... .. ..
L
I

As entered in AERO
Facility Name: Moncure Plywood,LLC Facility ID : 1900039
306 Corinth Road Permit: 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
Comments From Facility:
5/14/2013 —Operating Scenario Comments
OS OS24 : PM and PM-10 emissions are too small to show in AERO. See attached calcs.
5/14/2013 —Operating Scenario Comments
OS OS25 : PM and PM-10 emissions are too small to show in AERO. See attached calcs.
5/14/2013 —Operating Scenario Comments
OS OS 11 : Some criteria compound emissions are too small to show in AERO. See attached calcs.
5/14/2013 —Operating Scenario Comments
OS OS34 : PM and PM-10 emissions are too small to show in AERO. See attached calcs.
5/14/2013 —Operating Scenario Comments
OS OS3 : PM and PM-10 emissions are too small to show in AFRO. See attached calcs.
71

Division of Air
Home Emissions Flow Facility Totals ES-CD List User Manual Logoff
Operating Scenario Summary AERO
r IN/, Ne Vl
Emission Sources Emission Groups Control Devices Emission Release Points Operating Scenario Summary Closeout
PAGE INSTRUCTIONS Facility Id : 1900039 Data Year:2012
< Back Continue >
Find.OperatingScenario
OS Not Id Description Status
Operated
GR2 Green Veneer Stackers
OS32 Green Veneer Stackers
Add New Operating Scenario
G-24 Veneer dryers and heat source (wood burner) Q
OS26 Veneer dryers and heat source (wood burner)Ibs/SF, (Softwood)
OS27 Veneer dryers and heat source (wood burner) HAPS Ib/mmBtu,
(Softwood)
OS30 Veneer dryers and heat source(wood burner)Ibs/SF,(Hardwood)
OS31 Veneer dryers and heat source (wood burner)HAPS Ib/mmBtu, 4
(Hardwood)
Add New Operating Scenario
G-25 Ink and painting operations Q
OS5 Ink and painting operations
Add New Operating Scenario
G-27 Woodwaste Transfer system Q
OS20 Woodwaste Transfer(Rechipper)system 4
Add New Operating Scenario
ES-11 Green wood fuel storage silo Q
OS16 Green wood fuel storage silo
Add New Operating Scenario
ES-13-25HP 25 panel hot press Q
Add New Operating Scenario
ES-13-40HP 40 panel hot press Q
Add New Operating Scenario
ES-1 3-CC Curtain coater
Add New Operating Scenario
ES-1 3-PO Paper overlay operation Q
Add New Operating Scenario
ES-1 3-PS Plywood spreader
Add New Operating Scenario

ES03-CC Core composer with saw Q
Add New Operating Scenario
ES03-CS Core saw(green or dry veneer) Q
Add New Operating Scenario
ES03-PSS Panel sawing system Q
Add New Operating Scenario
ES03-SMS-1 String machine including saws Q
OS21 Dry Waste transfer system a
Add New Operating Scenario
ES03-SMS-2 String machine including saws Q
Add New Operating Scenario
ES03-SS Strip saw Q
Add New Operating Scenario
ESO4 Wood sander Q
OS12 wood sander
Add New Operating Scenario
ES12 Dry wood residual storage silo Q
OS17 drywood residual storage silo
Add New Operating Scenario
ES13-GMO Glue mixing operations consisting of two resin storage tanks and
four mixe
OS10 glue mi)ong,application and hot presses operations (Hardwood)
OS28 glue mixing,application and hot presses operations, (softwood)
Add New Operating Scenario
ES15 tongue and groove operations Q
OS19 tongue and groove operations
Add New Operating Scenario
ES16 Plywood waste hog Q
OS9 plywood hog
Add New Operating Scenario
ES20 Vat operations Q
OS18 Vat Operations: Heating of Blocks
Add New Operating Scenario
ES21 End sealer spray booth Q
OS33 End Sealer Spray Booth O
Add New Operating Scenario
ES22 Tongue and groove saw (plywood finishing) Q
OS34 Tongue and Groove Saw
Add New Operating Scenario
1-1 Bark hogging operations with two saws Q
OS2 Bark hogging operations
Add New Operating Scenario

I-11 hammer hog truck dump Q
OS25 Hammer hog truck dump-no controls
Add New Operating Scenario
1-12 dry waste truck dump Q
OS24 Dry Waste truck dump
Add New Operating Scenario
1-2 Core chipping and handling
OS3 Core chipping and handling operations
Add New Operating Scenario
1-3 Green veneer hogging Q
OS4 Green veneer hogging operations
Add New Operating Scenario
1-6 Plywood surface patching Q
OS6 Plywood surface patching
Add New Operating Scenario
1-7 Maintenance parts washers Q
OS7 Maintenance parts washer
Add New Operating Scenario
1-8 Veneer diverter exhaust cyclone Q
OS8 Veneer diverter exhaust cyclone 4
Add New Operating Scenario
IES19 Diesel-fired water pump(250 Horsepower maximum power Q
output)for emergenc
OS11 250 horsepower diesel-fired water pump
Add New Operating Scenario
< Back Continue>
' A
Feedback Top of Page

i
17
Moncure:Plywood LLC
..
Permit Limit Check
2012=Air.Emissions Inventory
URS ProjectNo.31828920
y
Source T22 Permit Limit 2012 Actual Emissions.. In Compliance?
PM _:: 15.3 8 lb/hr 905 lb/hr YES
-- Facility-wide PM 250 ton/yr : : 57.37 ton/yr: ... . YES
Facility-wide VOC I : 250 ton/yr I YES
11
FBB SO2 2.3 1 lb/M[rvMtu . . .. 0.025 lb/MMBtu .. I YES'
Acrolein 2.4 lb/hr 0.26 lb/hr YES.
:Arsenic 1.48 lb/yra a 0.11 lb/yr:: YES'..
rl
Benzene : . : 772.92 lb/yr. : 108.25 lb/ YES
16 YSBeryllium: 26.41 lb/"r 1
yr
..
Cadmium :::35,21b/yr 0.58lb/yr .::::: YES:
Chlorine :101.13lb/day 0.32lb/day: : YES''
ES09 Chlorine 27.02 lb/hr_ OOL 1b/hr 7 7 7YES
Formaldeh'de:. 3.77 lb/hr. .. 0.'11 lb/hr YES
Hydro en Chloride ::21.02 lb/hr 0.01 lb/hr...
Manganese ... .. 83.6 lb/day. 0.65.lb/day' " YES
Nickel(metal): ' 16.19 lb/day :::0:01 lb/day
. Phenol 6.74lb/hr' 0.041b/hr . YES
Vinyl Chloride 38; yr 27.3 b yr:: YES'
Acrolein: : : 2.4 lbnir :0:26 lb/hr YES
:Arsenic :::: 1.48 lb/yr :::_= :: 0.11 lb/yr... : : :: -
.
Benzene .772.92 lb/yr 108.25 lb/ YES
0.-1.6 lb/ r Beryllium.. ::: :: 26.41 lb/yT :: y
Cadmium 35.2 lli/yr 0:58 lb/yr YES.
.:::'Chlorine :::: :101.13 lb/day :::: . 0.32 lb/day:':`: YES:::.
ES 10 Chlorine 27.02 lb/hr.. : 0.01 _lb/hr ..YES
Formaldeh :de:' 3.77 lb/hf 0.11 lb/hr ::= : YES
I Hydrogen Chloride ::2.1.02 lb/hi' 0.01 lb/hr YES.
-::Manganese 83:6 lb/day = : : 0.65 Ib/day: : YES
Nickel(metal): : : 16.19 lb/day: 001 lb/day YES
i Phenol 6.74 lb/hr. .. 0.04 lb/hr YES
V.in'1'Chloride 3:8;656 lb/ r ... ::: :: 27.35 lb/ YES- 7 =
Formaldehyde: 2.33 :Ib/hr' :: ::0061b/hr YES
ES 13 28.62 Ib%lir 0.12 lb/hr YES Phenol

I
:.:
Moncure PlywoodLLC ... .
Annual Activity acid Usage Information
2012 Air Emissions Inventory
URS Project No.31828920
Activity and Usage 2012 Annual Amount
Description::.:. .
L-1 Plywood Production
Hardwood Plywood Production 71,248,000 fe:(3/8")
1 Softwood Pl ood Production 46,285,000 fe(3/8")
Plywood ood Press Hours of eration:: :6,954 hours
Sander Production 45.1326,000 ftz(3/8")'
T&G Saw Production 53,000 fe:(3/9")
T&G Saw Hours of.Operation 30 hours
Lo Throu h ut
Pine Los 62,771.tons
�. . Gum Los 114,383:tons
Poplar.Logs 20,536 tons
Piaet wide Fuel Combustion':
Boiler Hours of Operation 8,399:hours,
Total Dry Wood Combusted' 3,640 ton(as fired)
Dr
y: Heat Content : . : .• . 7,776 Btu/Ib
Total Dry Wood Combusted: 56,606 MMBtu/yr
Green Chi s-Combusted 3,116 tons chips
Green Chips Heat Content z 4,541:Btu/lb
Total Green Chips Combusted.:: .: :28,300 MMBtu'—.
Total Hog Fuel Combusted : . : 20,625 ton as fired
,5703 Poplar Bark Heat ContentZ Btu/lb
Gum Bark Heat Content 4,952 Btu/]b
Pine:Bark Heat Content :: :: : :: 4,018 Btu/lb ::
Total Hog Fuel Combusted 199,089 MMBtu
:MMBtu
Total Green Fuel:Combusted 22T,389
�. . .
Total of all fuel combusted 283,995 MMBtu
Boiler Efficiency86.0%
250 HP Diesel Fired Water Pump
.205. al/
. . .: rom
44:hr/yr .
Miscellaneous
Veneer Diuerter :: 185,015 ton/ r
Hammer Hog Truck Dump 4344:ton! r.
Dry Waste Trick Durnp 91:ton/
� I
Core Chipping and Handling :: . : 976 tonlyr
Green Veneer Hogging Operations 34,624 ton/yr
Maintenance Parts Washer :110: al/ :
End Seal Paint: ; = : : 3-,300:gal/yr
Paint Usage(Logo painting) .::::: ::::: 866 al/ r
Ink Usage . 295 al/ r
Plywood Surface:Patch' 18'810:gall :
Cores Sold in 2012 680'800:cores
. . . Ash:.:. :. .. . .
Total Wood Ash
586 tons
l ......
Total Wood Ash.sent offsite 586 tons
PF Resin Usa a . . .. "
PF Resin Application Rate'. 27 Tons/MMSF
OF Resin Usage 4,813 tons
1. Bark fired is:calcolated based on log usage:aad"peicentage 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:froin Chester Plywood(sisterpfant).
2. Heat Content is Chester Plywood fuel analysis data.