AQ_F_1900039_20140804_EI_Cmb-EI-File

2013 Emissions Inventory Review / Data Tracking Form
Facility Name: Moncure'Plywood Facility ID: 1900039
Facility Assigned to: Data Entry: Chatham County
Classification: Maureen Conner Confidential Copy Submitted?
Title V ❑ YES
JI NO
Initial Review/Data Entry
Enter date received into ED. Date Received: ( wo_ �26 9_D !4
:07 Assigned to appropriate individual. Date Assigned: Aix- 26 Date Due:
❑ Paver copy submitted: One copy received with supporting documentation,certification form signed by responsible official,and
appears generally complete;OR
Electronic copy submitted: All supporting documentation and certification form(with time/date stamp)signed by responsible
official has been received.
Comments:
Inventory Review
❑ All forms and supporting documentation appear,to be complete if paper submission(check ED OS data if electronic).
❑ Contact,address,phone number changes entered into I-Beam/Facilities if necessary.
❑ All known operating scenarios,control devices,and emission release points have been entered for each emission source(permitted,,,,
insignificant,and unpermitted)or note that the emission source was not operated or not required to report.
❑ Evaluate"U"sources for significance and address according to policy.
❑ Calculations/forms appear to add up correctly.
❑ All compliance issues are being addressed(e.g.Toxics limits,above TV thresholds,large emissions increase/decrease,installation
without a permit).
❑ All volatile HAPs/TAPS were included in the VOC total.
❑ Calculations and control efficiencies appear correct. Emission factors are the best available and most current factors appropriate
for the reporting facility(e.g.stack testing,AP-42,etc.).
❑ Review facility comments and address any issues.
❑ Update ED(Data Entry Main)if additional information is required(corrections due date and date received).
❑ Check all ED QA/QC reports.
❑ Comparison with previous emission inventory must be made and outliers(> 10%)must be investigated and explained.
❑ Put inventory review comments and summarize any changes in ED-Data Entry Main"DAQ internal comments".
❑ Print and attach the facility total report.
Date Review Complete: to- �0-70 14 Signature: l G •�- ( � C��.
Date Submitted to EI Coordinator:/ io-i-A-2o I4
Date Approved: , I I Initials: b*

Facility Total CY 2013 Emission Summary Recorded in ED Facility ID#: 1900039
Facility Name: Moncure Plywood Permit#(s): 03424T23
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 2013 CY 2012 Demini- %
from ED from Fees mus Change
CO CO 29.28 27.29 0.5 7.3%
NOx NOx 44.14 38.94 0.5 113.4% ,/
PM(TSP) TSP 66.42 57.64 0.5 115.2%
PM10 PM10 66.40 57.64 0.5 115.2%
PM2.5, PM2.5 55.20 52.93 0.5 4.3%
S02 S02 0.700000 3.55 0.5 1-80.3%"/
VOC VOC 63.30 51.77 0.5 22.3%
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPs) (Pounds/Year)
Pollutant CAS CY 2013 CY 2012 Demini- %
from ED from Fees mus Change
Antimony & Compounds (total mass, inc elemental SB) Not 2.24 10.0 I N/A
Reported
Antimony Unlisted Compounds-Speck Compound SBC-other Not 2.24 10.0 N/A
(Component of SBC) Reported
Arsenic & Compounds (total mass of elemental AS, arsine and 1.39 0.210160 0.01 I
561.4%
all inorganic compounds)
Arsenic Unlisted Compounds-Specify Compound ASC-Other 1.39 0.210160 0.01 . 563.6%
(Component of ASC)
Beryllium & compounds (Total mass) Not 0.312390 1,0 I N/A
Reported
Beryllium Metal(unreacted) (Component of BEC) 7440-41-7 Not 0.312390 1.0 N/A
Reported
10/13/2014 Page 1 of 5

Facility Total CY 2013 Emission Summary Recorded in ED Facility ID #: 1900039
Facility Name: Moncure Plywood Permit#(s): 03424T23
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPs) (Pounds/Year)
Pollutant CAS CY 2013 CY 2012 Demini- %
from ED from Fees mus Change
Cadmium & compounds (total mass includes elemental metal) 2.06 ' 7.52 0.1 I -72.6%
Cadmium Metal, elemental,'unreacted(Component 7440-43-9 2.06 7.52 0.1 -72.6%
of CDC)
Chromium-All/Total(includes Chromium (VI) categories, 13.41 5.96 0.1 1125.0%
metal and others)
Chromic acid(VI) (Component ofSolCR6& CRC) 7738-94-5 3.02 0.993980 0.01 1203.7%
Chromium Unlisted Compounds -Specify CRC-Other 10.39 4.97 0.1 109.2%
Compound(Component of CRC)
Chromium (VI)Soluble Chromate Compounds (Component of 3.02 0.993980 0.01 I
203.8%
CRC)
Chromic acid(VI) (Component of SolCR6& CRC) 7738-94-5 3.02 0.993980 0.01 1203.7%.
Cobalt& compounds Not 1.85 1.0 N/A
Reported
Cobalt Unlisted Compounds-Specify Compound COC-other Not 1.85 1.0 N/A
(Component of CDC) Reported
Lead& compounds 6.67 13.63 1.0 -51.1%
Lead Unlisted Compounds-Specify Compound PBC-other 6.67 13.63 10.0 -51.1.°%
(Component of PBQ
Manganese & compounds 1,078.45 454.39 10.0 137.3%
Manganese Unlisted Compounds -Specify MNC-Other 1,078.45 454.39 10.0 137.3%
Compound(Component of MNQ
Mercury & Compounds-all total mass includes Hg Vapor 0.498080 0.993980 0.001 1 -49.9%,l
Mercury, vapor (Component of HGC) 7439-97-6 0.498080 0.993980 0.001 -49.9%
Nickel& Compounds,sum total mass includes elemental 5.07 9.37 1.0 I -45.9%
Nickel metal (Component ofNIC) 7440-02-0 5.07 9.37 1.0 -45.9%
Polycyclic Organic Matter (7 PAH Compounds for NIF) Not 0.738400 1.0 N/A
Reported
Benzo(a)pyrene (Component of 833291POMTV& 50-32-8 Not 0.738400 1.0 N/A
5655317PAH) Reported
10/13/2014 Page 2 of 5

Facility Total CY 2013 Emission Summary Recorded in ED Facility ID #: 1900039
Facility Name: Moncure Plywood Permit#(s): 03424T23
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPS) (Pounds/Year)
Pollutant CAS CY 2013 CY 2012 Demini-
from ED from Fees mus Change
Polycyclic Organic Matter(Specific Compounds from OAQPS 3.53 28.29 1.0 87.5%
or TV)
Benzo(a)pyrene (Component of 833291POMTV& 50-32-8 Not 0.738400 1.0 N/A
5655317PAH) Reported
Naphthalene (Component of 833291POMTi) 91-20-3 3.53 27.55 1.0 -87.2%
Acetaldehyde 75-07-0 2,352.32 5,051.54 10.0 -53.4%
Acrolein 107-02-8 342.28 371.04 10.0 -7.8%
Benzene 71-43-2 182.10 216.53 1.0 -15.9%
Carbon tetrachloride 56-23-5 1.10 12.78 1.0 -91.4%
CFC-11 (Trichlorofluoromethane) 75-69-4 Not 11.64 100.0 N/A
Reported
Chlorine 7782-50-5 342.16 224.36 100.0 52.5%
Chlorobenzene 108-90-7 Not - 9.37 10.0 N/A
Reported
Chloroform 67-66-3 Not 7.95 100.0 N/A
Reported
Cumene 98-82-8 - 1,499.66 2,097.91 100.0 -28.5a/o
DEHP (Di(2-ethylhexyl)phthalate) 117-81-7 Not 0.013350 10.0 N/A
Reported
Dinitrophenol, 2,4- 51-28-5 Not 0.051120 0.1 N/A
- Reported
Ethyl benzene 100-41-4 Not 8.80 100.0 N/A
Reported
Ethyl chloride (chloroethane) 75-00-3 a_ 24.90 55.39 10.0 1-55.1%
Ethylene dichloride (1,2-dichloroethane) 107-06-2 38.17 86.02 1.0 1-55.6%
Formaldehyde 50-00-0 2,354.13 2,280.33 10.0 3.2%
Hexachlorodibenzo-p-dioxin 1,2,3,6,7,8 57653-85-7 0.692980 Not 0.00001 N/A
Reported
Hydrogen chloride (hydrochloric acid) 7647-01-0 149.86 159.04 100.0 -5.8%
MEK(methyl ethyl ketone, 2-butanone) 78-93-3 121.89 318.78 100.0 1-61.8%',
10/13/2014 Page 3 of 5

Facility Total CY 2013 Emission Summary Recorded in ED Facility ID#: 1900039
Facility Name: Moncure Plywood Permit#(s): 03424T23
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPs) (Pounds/Year)
Pollutant CAS CY 2013 CY 2012 Demini- %
from ED from Fees mus Change
Methanol (methyl alcohol) 67-56-1 ---8,461.97 11,960.94 1,000.0 -29.3%
Methyl bromide (bromomethane) 74-83-9 -�' 59.23 83.70 1.0 -29.2'%
Methyl chloride (chloromethane) 74-87-3 11.52 6.53 1.0 76.4%
Methyl chloroform 71-55-6 Not 8.80 100.0 N/A
Reported
Methylene chloride 75-09-2 _- 53.07 74.73 1.0 1-29.0%'/
MIBK(methyl isobutyl ketone) 108-10-1 184.87 645.57 10.0 -71..4%
Nitrophenol, 4- 100-02-7 Not 0.031240 10.0 N/A
Reported
Pentachlorophenol 87-86-5 Not 0.014480 1.0 NIA
Reported
Perchloroethylene (tetrachloroethylene) 127-18-4 Not 10.79 100.0 N/A
Reported
Phenol 108-95-2 1,742.00 1,476.73 100.0 18.0%
Phosphorus Metal, Yellow or White 7723-14-0 y a 2,360.46 7.67 1.0 3 0,683.9°
Polycyclic Organic Matter(Inc PAH, dioxins, etc.NCPOM 9.67 35.50 1.0 -72.8%
&AP 42 historic)
Propionaldehyde 123-38-6 - 79.19 232.93 10.0 -66.0%
Propylene dichloride (1,2-dichloropropane) 78-87-5 Not 9.37 10.0 N/A
Reported
Selenium Compounds SEC Not 0.795190 10.0 N/A
Reported
Styrene 100-42-5 Not 152.06 100.0 N/A
Reported
TCE (trichloroethylene) 79-01-6 Not 8.52 1,000.0 N/A
Reported
Toluene 108-88-3 Not 320.83 100.0 N/A
Reported
Trichlorobenzene, 1,2,4- 120-82-1 113.25 160.28 100.0 -29.3%
Trichlorophenol, 2,4,6- 88-06-2 Not 0.006250 1.0 N/A
Reported
10/13/2014 Page 4 of 5

Facility Total CY 2013 Emission Summary Recorded in ED Facility ID #: 1900039
Facility Name: Moncure Plywood Permit#(s): 03424T23
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPS) (Pounds/Year)
Pollutant CAS CY 2013 CY 2012 Demini- %
from ED from Fees mus Change
Vinyl acetate 108-05-4 Not 8.19 100.0 N/A.
Reported
Vinyl chloride 75-01-4 38.97 54.69 0.1 1-28.8%"
Viriylidene chloride 75-35-4 58.64 Not 0.1 N/A
Reported
Xylene (mixed isomers) 1330-20-7 117.36 338.85 100.0 1-65.4%,--
Largest Individual HAP Methanol (methyl alcohol) 8,461.97 lbs
Total HAP Emissions 21,687.95
lbs -
DAQ's Comments Regarding Inventory
ES15/OS19 is no longer a source on the permit T22 issued in June 2011,therefore this source should be end dated.From
CY 2012 to CY 2013 the facility increased their veneer drying by 23%for softwoods and 54%for hardwoods which
accounts for the change in emissions. Specific changes in emissions are attached to paper copy of the facility's AQEI.
10/14/2014 Page 5 of 5

Emissions by Operating Scenario
for
NOx
2013 Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario Cy 2��2 (Tons/Yr) Source ID
31 Veneer dryers and heat 28.56
source(wood burner)
HAPS lb/mmBtu,
(Hardwood)
ES01-A
ES01-B
ES09
ES10
27 Veneer dryers and heat S . 3 15.40
source (wood burner)
HAPS lb/mmBtu,
(Softwood)
ES01-A
ES01-B
ES09
ES10
11 250 horsepower diesel- a d �0 0.13
fired water pump
IES 19
35 250 HP Diesel Fired Water Pump#2-IES23 0.05
IES 19
33 q9 Total: 44.14

Emissions by Operating Scenario
for
PM(TSP)
2013 Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario C\4 20 i 2 (Tons/Yr) Source ID
31 Veneer dryers and heat 2 15 21.77
source (wood burner)
HAPS lb/mmBtu,
(Hardwood)
ES01-A
ES01-B
ES09
ES 10
21 Dry Waste transfer system 1 .cog 15.35
ES03-SMS
27 Veneer dryers and heat 3, =t LI 11.73
source (wood burner)
HAPS lb/mmBtu,
(Softwood)
ES01-A
ES01-B
ES09
ES 10
10 glue mixing, application 8.36
and hot presses
operations(Hardwood)
ES 13-GM(
28 glue mixing, application ` .20 ^ q . 4.51
and hot presses
operations, (softwood)
ES 13-GM(
8 Veneer diverter exhaust 2 5 2.30
cyclone
I-8
32 Green Veneer Stackers �� '(` ! 'i. 0.61
I-10
I-9
17 dry wood residual storage SS 0.60
silo
ES 12
20 Woodwaste Transfer o,4 �- 0.47
(Rechipper) system

Emissions by Operating Scenario
for
PM(TSP)
2013 Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario (Tons/Yr) Source ID
ES 14
ES17
9 plywood hog 0.36
O IU ES16
12 wood sander N 0.22
ESO4
33 End Sealer Spray Booth p .09 0.08
ES21
4 Green veneer hogging v S 0.02
operations
I-3
2 Bark hogging operations o O3 0.01
1-1
11 250 horsepower diesel- 0.01
fired water pump (Z
IES 19
16 Green wood fuel storage O. O 1 0.01
silo
IES-GWS
34 Tongue and Groove Saw N 0.01
� ES22
5 Total: 66.42

Emissions by Operating Scenario
for
PM10
2013 Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario Cy 201 Z (Tons/Yr) Source ID
31 Veneer dryers and heat Z 1 , �S 21.77
source (wood burner)
HAPS lb/mmBtu,
(Hardwood)
ES01-A
ES01-B
ES09
ES 10
21 Dry Waste transfer system S �O 15.35
ES03-SMS
27 Veneer dryers and heat 3 q . :. . 11.73
source (wood burner) v
HAPS lb/mm.Btu,
(Softwood)
ES01-A
ES01-B
ES09
ES 10
10 glue mixing, application Q3-It ^ 1 'i- 8.36
and hot presses
operations(Hardwood)
ES 13-GM(
28 glue mixing, application ZO s , "/, 4.51
and hot presses
operations, (softwood)
ES 13-GM(
8 Veneer diverter exhaust Z q S 2.30
cyclone
I-8
32 Green Veneer Stackers 0.61
I-10
I-9
17 dry wood residual storage 0.60
silo s S
ES12
20 Woodwaste Transfer 0.47
(Rechipper) system v , Gd

Emissions by Operating Scenario
for
PM10
2013 Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario C- 2-0 Z (Tons/Yr) Source ID
ES14
ES17
o • �o
9 plywood hog 0.36
ES16
12 wood sander U 2. 0.22
ESO4
33 End Sealer Spray Booth C.) ' DC� 0.08
ES21
2 Bark hogging operations 3 0.01
1-1
4 Green veneer hogging G ' S 0.01
operations
I-3
11 250 horsepower diesel- 0.01
fired water pump
IES 19
16 Green wood fuel storage 0.01
silo G 2
IES-GWS
S (o a1 Total: 66.40
--�' �,5. Z'i,

Emissions by Operating Scenario
for
S02
2013 Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario G y 2 p\2 (Tons/Yr) Source ID
31 Veneer dryers and heat Z• 1 S 4 q �• 0.45
source(wood burner)
HAPS lb/mmBtu,
(Hardwood)
ES01-A
ES01-B
ES09
ES 10
27 Veneer dryers and heat 1 al0 32 ' -�' 0.24
source (wood burner)
HAPS lb/mmBtu,
(Softwood)
ES01-A
ES01-B
ES09
ES 10
11 250 horsepower diesel- Y-1 0.01
fired water pump
IES19
Total: 0.70
A/ 3 -/.

Emissions by Operating Scenario
for
VOC
2013Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario Cy 2d�2 (Tons/Yr) Source ID
26 Veneer dryers and heat 3. 9 %, 39.89
source (wood burner)
lbs/SF, (Softwood)
ESO1-A
ESO1-B
ES09
ES 10
28 glue mixing, application S . Cc 2 � � . -1 '/, 7.53
and hot presses
operations, (softwood)
ES 13-GM(
30 Veneer dryers and heat Co 4� t 5.60
source (wood burner)
lbs/SF, (Hardwood)
ESO1-A
ESO1-13
ES09
ES10
10 glue mixing, application Co Z 4.27
and hot presses
operations(Hardwood)
ES 13-GM(
12 wood sander N YZ_ 2.95
ES04
18 Vat Operations: Heating of Z S 2.24
Blocks
ES20
5 Ink and painting operations G Z 0.55
I-4
I-5
7 Maintenance parts washer 0.19
I-7
33 End Sealer Spray Booth 0.05
ES21
6 Plywood surface patching 0.01
Z . � �- I-6

Emissions by Operating Scenario
for
VOC
2013 Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario C-�-? 20 t2 (Tons/Yr) Source ID
11 250 horsepower diesel- 0.01
fired water pump
IES 19
34 Tongue and Groove Saw 0.01
ES22
S 1 -� Total: 63.30
t

Emissions by Operating Scenario
for
Acetaldehyde
2013 Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario C`1 -20\2 (Pounds/Yr) Source ID
26 Veneer dryers and heat � �13 dt ,23 �,^ 3,0Y0Ib 1,081.87
source (wood burner)
lbs/SF, (Softwood)
ES01-A
ES01-B
ES09
ES 10
18 Vat Operations: Heating of SS2 ,`� �i`�10�� w 601.09
Blocks
ES20
30 Veneer dryers and heat 3 4 �' � 437.41
source(wood burner)
lbs/SF, (Hardwood)
ES01-A
ES01-B
ES09
ES10
28 glue mixing, application ` q4 , �{p .�.N �b� 162.73
and hot presses
operations, (softwood)
ES 13-GM(
12 wood sander 69.03
ESO4
34 Tongue and Groove Saw 0.12
ES22
11 250 horsepower diesel- 0.04
fired water pump
IES 19
35 250 HP Diesel Fired Water Pump#24ES23 0.02
IES 19
Cam'ps I ,S Total: 2,352.32

Emissions by Operating Scenario
for
Arsenic Unlisted Compounds - Specify Compound (Component of ASC)
2013 Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario C•,1 20\—L (Pounds/Yr) Source ID
31 Veneer dryers and heat rj t 3 �� 0.91
source (wood burner)
HAPS lb/mmBtu,
(Hardwood)
ES01-A
ES01-B
ES09
ES 10
27 Veneer dryers and heat 0.49
source(wood burner) G D C6
HAPS lb/mmBtu,
(Softwood)
ES01-A
ES01-B
ES09
ES10
CU. 2 Total: 1.39

Emissions by Operating Scenario
for
Benzene
2013Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario C-1 2612 (Pounds/Yr) Source ID
26 Veneer dryers and heat 157.77
source(wood burner)
lbs/SF, (Softwood)
ES01-A
ES01-B
ES09
ES10
30 Veneer dryers and heat `4G ' a�' �N ZS 1b 24.25
source (wood burner)
lbs/SF, (Hardwood)
ES01-A
ES01-B
ES09
ES 10
11 250 horsepower diesel- 0.05
fired water pump
IES 19
35 250 HP Diesel Fired Water Pump#2-IES23 0.02
IES 19
Total: 182.10

Emissions by Operating Scenario
for
Cadmium Metal, elemental, unreacted (Component of CDC)
2013Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario c y zo�Z (Pounds/Yr) Source ID
31 Veneer dryers and heat U� 1.34
source(wood burner)
HAPS lb/mmBtu,
(Hardwood)
ES01-A
ES01-B
ES09
ES10
27 Veneer dryers and heat 0.72
source (wood burner)
HAPS lb/mmBtu,
(Softwood)
ES01-A
ES01-B
ES09
ES10
•S Z Total: 2.06
,J, -72. !o %-j

Emissions by Operating Scenario
for
Carbon tetrachloride
2013Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario Cy 20k2. (Pounds/Yr) Source ID
31 Veneer dryers and heat S y,� 7 \b 0.72
source (wood burner)
HAPS lb/mmBtu,
(Hardwood)
ES01-A
ES01-B
ES09
ES 10
27 Veneer dryers and heat 0.39
source (wood burner) S • U 3 �i g /o b
HAPS lb/mmBtu,
(Softwood)
ES01-A
ES01-B
ES09
ES 10
I2 Total: 1.10
,�a 1 4 '/41

Emissions by Operating Scenario
for
Chlorine
2013 Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario 2,0\2 (Pounds/Yr) Source ID
31 Veneer dryers and heat 3 222.33
source (wood burner)
HAPS lb/mmBtu,
(Hardwood)
ES01-A
ES01-B
ES09
ES 10
27 Veneer dryers and heat 119.83
source (wood burner) 5
HAPS lb/mmBtu,
(Softwood)
ES01-A
ES01-B
ES09
ES10
22 4 . 3 Co Total: 342.16
52.5 •/,

Emissions by Operating Scenario
for
Chromium Unlisted Compounds - Specify Compound (Component of CRC)
2013 Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario C 2U (Pounds/Yr) Source ID
31 Veneer dryers and heat 3 3 b 6.75
source (wood burner)
HAPS lb/mmBtu,
(Hardwood)
ES01-A
ES01-B
ES09
ES10
27 Veneer dryers and heat 2- 3.64
source (wood burner)
RAPS lb/mmBtu,
(Softwood)
ES01-A
ES01-B
ES09
ES 10
q Total: 10.39

Emissions by Operating Scenario
for
Cumene
2013 Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario cy Zo12 (Pounds/Yr) Source ID
26 Veneer dryers and heat 1,49(o,21 -44S.,A1 ib 752.80
source (wood burner)
lbs/SF, (Softwood)
ES01-A
ES01-B
ES09
ES10
30 Veneer dryers and heat 746.86
source (wood burner) '
lbs/SF, (Hardwood)
ES01-A
ES01-B
ES09
ES10
Z,oq Total: 1,499.66

Emissions by Operating Scenario
for
Ethyl chloride (chloroethane)
2013 Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario C� 2v12 (Pounds/Yr) Source ID
30 Veneer dryers and heat 20.07
source (wood burner)
lbs/SF, (Hardwood)
ES01-A
ES01-B
ES09
ES10
26 Veneer dryers and heat 4.82
source (wood burner)
lbs/SF, (Softwood)
ES01-A
ES01-B
ES09
ES10
Total: 24.90

Emissions by Operating Scenario
for
Ethylene dichloride (1,2-dichloroethane)
2013 Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario C"q 20�1 (Pounds/Yr) Source ID
30 Veneer dryers and heat �9d S �^3p 3 0.7 8
source (wood burner)
lbs/SF, (Hardwood)
ES01-A
ES01-B
ES09
ES10
26 Veneer dryers and heat ZS ( 1 14 ,�)0 e +, 7.39
source (wood burner)
lbs/SF, (Softwood)
ES01-A
ES01-B
ES09
ES10
g (o, 32 Total: 38.17

Emissions by Operating Scenario
for
Lead Unlisted Compounds - Specify Compound (Component of PBQ
2013Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario c-1-J 'ZG Z (Pounds/Yr) Source ID
31 Veneer dryers and heat . 2cp 4.33
source (wood burner)
HAPS lb/mmBtu,
(Hardwood)
ES01-A
ES01-B
ES09
ES10
27 Veneer dryers and heat ,3� low 2.34
source (wood burner)
HAPS lb/mmBtu,
(Softwood)
ES01-A
ES01-B
ES09
ES 10
i �. (0 3 Total: 6.67

Emissions by Operating Scenario
for
Manganese Unlisted Compounds - Specify Compound (Component of MNQ
2013 Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario Gy ZU12 (Pounds/Yr) Source ID
31 Veneer dryers and heat Z 25' 3 700.75
source (wood burner)
HAPS lb/mmBtu,
(Hardwood)
ES01-A
ES01-B
ES09
ES10
27 Veneer dryers and heat 377.70
source(wood burner)
HAPS lb/mmBtu,
(Softwood)
ES01-A
ES01-B
ES09
ES 10
,A SA 3 Total: 1,078.45

Emissions by Operating Scenario
for
MEK (methyl ethyl ketone, 2-butanone)
2013 Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario G--1 X12- (Pounds/Yr) Source ID
30 Veneer dryers and heat 1 �� q 3 y�g3 1\0 84.47
source (wood burner)
lbs/SF, (Hardwood)
ES01-A
ES01-B
ES09
ES10
28 glue mixing, application 36.60
and hot presses
operations, (softwood)
ES 13-GM(
27 Veneer dryers and heat q Z� yvgd�b 0.82
source(wood burner)
HAPS lb/mmBtu,
(Softwood)
ES01-A
ES01-B
ES09
ES10
Total: 121.89

Emissions by Operating Scenario
for
Mercury, vapor (Component of HGQ
2013 Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario C� 2ot (Pounds/Yr) Source ID
31 Veneer dryers and heat 0.32
source (wood burner)
HAPS lb/mmBtu,
(Hardwood)
ES01-A
ES01-B
ES09
ES 10
27 Veneer dryers and heat d , 3� 0.17
source (wood burner)
HAPS lb/mmBtu,
(Softwood)
ES01-A
ES01-B
ES09
ES 10
c' �1 Total: 0.50
a��

Emissions by Operating Scenario
for
Methanol (methyl alcohol)
2013Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario C-A -Zo\2 (Pounds/Yr) Source ID
28 glue mixing, application MW 2,727.22
and hot presses
operations, (softwood)
ES13-GM(
26 Veneer dryers and heat �, (a . Z (O \\oo 1,861.72
source (wood burner)
lbs/SF, (Softwood)
ES01-A
ES01-B
ES09
ES10
10 glue mixing, application Z ,2-41; qg 1,831.61
and hot presses
operations (Hardwood)
ES 13-GM(
18 Vat Operations: Heating of �S a yN i oU �b 944.75
Blocks
ES20
30 Veneer dryers and heat SCp �. pp\�o 793.70
source (wood burner)
lbs/SF, (Hardwood)
ES01-A
ES01-B
ES09
ES10
12 wood sander 301.47
ESO4
34 Tongue and Groove Saw 1.50
ES22
l l C 1 (oG , 4 Total: 8,461.97
-Z

Emissions by Operating Scenario
for
Methyl bromide (bromomethane)
2013 Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario G�-t 20\2— (Pounds/Yr) Source ID
26 Veneer dryers and heat 29.71
source (wood burner)
lbs/SF, (Softwood)
ES01-A
ES01-B
ES09
ES10
30 Veneer dryers and heat 23 iq 29.52
source (wood burner)
lbs/SF, (Hardwood)
ES01-A
ES01-B
ES09
ES10
8 3 - Total: 59.23

Emissions by Operating Scenario
for
Methyl chloride (chloromethane)
2013Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario C—`-4 (Pounds/Yr) Source ID
31 Veneer dryers and heat 3 7.49
source (wood burner)
HAPS lb/mmBtu,
(Hardwood)
ES01-A
ES01-B
ES09
ES10
27 Veneer dryers and heat 2 5� �1 \ \ 4.03
source (wood burner)
HAPS lb/mmBtu,
(Softwood)
ES01-A
ES01-B
ES09
ES10
Total: 11.52

Emissions by Operating Scenario
for
Methylene chloride
2013 Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario Zo\'L (Pounds/Yr) Source ID
26 Veneer dryers and heat 53, AA 26.64
source (wood burner)
lbs/SF, (Softwood)
ES01-A
ES01-B
ES09
ES10
30 Veneer dryers and heat 2 Z� 26.43
source (wood burner)
lbs/SF, (Hardwood)
ES01-A
ES01-B
ES09
ES10
�3 Total: 53.07

Emissions by Operating Scenario
for
MIBK (methyl isobutyl ketone)
2013Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario G-i 20\2 (Pounds/Yr) Source ID
30 Veneer dryers and heat y� �p\gyp r 80.54
source (wood burner)
lbs/SF, (Hardwood)
ES01-A
ES01-B
ES09
ES10
27 Veneer dryers and heat , 67.50
source (wood burner) N 2
HAPS lb/mmBtu,
(Softwood)
ES01-A
ES01-B
ES09
ES10
28 glue mixing, application k! N 3--D 1 b 36.83
and hot presses
operations, (softwood)
ES 13-GM(
(a-A 15. Total: 184.87
2 � 4(to kb

Emissions by Operating Scenario
for
Naphthalene (Component of 83329/POMTV)
2013Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario C,y -Zr1 Z (Pounds/Vr) Source ID
31 Veneer dryers and heat a, 14 Il0 2.29
source (wood burner)
HAPS lb/mmBtu,
(Hardwood)
ESO 1-A
ESO1-B
ES09
ES10
27 Veneer dryers and heat 1.23
source (wood burner)
HAPS lb/mmBtu,
(Softwood)
ESO 1-A
ESO1-B
ES09
ES10
11 250 horsepower diesel- 0.00
fired water pump
IES 19
35 250 HP Diesel Fired Water Pump #2-IES23 0.00
IES 19
2 SS Total: 3.53

Emissions by Operating Scenario
for
Nickel metal (Component of NIQ
2013 Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario cy 2o12- (Pounds/Yr) Source 1D
31 Veneer dryers and heat 3.29
source (wood burner)
HAPS lb/mmBtu,
(Hardwood)
ES01-A
ES01-B
ES09
ES10
27 Veneer dryers and heat 1.77
source (wood burner) 3
HAPS lb/mmBtu,
(Softwood)
ES01-A
ES01-B
ES09
ES 10
Total: 5.07

Emissions by Operating Scenario
for
Phenol
2013 Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario C`-( 20\2 (Pounds/Yr) Source ID
10 glue mixing, application -�cUz 3 .a /�•c����0 1,329.80
and hot presses
operations (Hardwood)
ES 13-GM(
26 Veneer dryers and heat 3 d2 ? 153.72
source (wood burner)
lbs/SF, (Softwood)
ES01-A
ESOI-B
ES09
ES10
30 Veneer dryers and heat 2 �O k y 3J�� 136.33
source (wood burner)
lbs/SF, (Hardwood)
ESO1-A
ESO1-B
ES09
ES10
28 glue mixing, application \b 122.16
and hot presses
operations, (softwood)
ES 13-GM(
q��,� Total: 1,742.00

Emissions by Operating Scenario
for
Phosphorus Metal, Yellow or White
2013 Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario G-1 Zp Z (Pounds/Yr) Source ID
31 Veneer dryers and heat ,�S4 1,533.78
source (wood burner)
HAPS lb/mmBtu,
(Hardwood)
ES01-A
ES01-B
ES09
ES10
27 Veneer dryers and heat 3 Z 23 Vb 826.68
source (wood burner)
RAPS lb/mmBtu,
(Softwood)
ES01-A
ES01-B
ES09
ES10
-� �� Total: 2,360.46

Emissions by Operating Scenario
for
Polycyclic Organic Matter (Inc PAH, dioxins, etc. NC & AP 42 historic)
2013 Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario GY 2012 (Pounds/Yr) Source ID
31 Veneer dryers and heat Z S 6.28
source (wood burner)
HAPS lb/mmBtu,
(Hardwood)
ES01-A
ES01-B
ES09
ES10
27 Veneer dryers and heat 3 S . 3.38
source(wood burner)
HAPS lb/mmBtu,
(Softwood)
ES01-A
ES01-B
ES09
ES 10
11 250 horsepower diesel- 0.01
fired water pump
IES 19
35 250 HP Diesel Fired Water Pump#24ES23 0.00
IES 19
35. S O Total: 9.67

Emissions by Operating Scenario
for
Propionaldehyde
2013 Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario L`1 W\2. (Pounds/Yr) Source ID
30 Veneer dryers and heat 1 °i. , �02 --f 4 b 75.94
source (wood burner)
lbs/SF, (Hardwood)
ESO 1-A
ES01-B
ES09
ES10
27 Veneer dryers and heat 3.25
source (wood burner)
HAPS lb/mmBtu,
(Softwood)
ES01-A
ESO1-B
ES09
ES10
Z2J2 1:713 Total: 79.19

Emissions by Operating Scenario
for
Trichlorobenzene, 1,2,4-
2013 Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario C� 2D\2 (Pounds/Yr) Source ID
f
26 Veneer dryers and heat \4. g i b 56.80
source (wood burner)
lbs/SF, (Softwood)
ES01-A
ES01-B
ES09
ES10
30 Veneer dryers and heat 56.45
source (wood burner)
lbs/SF, (Hardwood)
ES01-A
ES01-B
ES09
ES 10
I Co U -ZS Total: 113.25

Emissions by Operating Scenario
for
Vinyl chloride
2013 Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario 2CA-L (Pounds/Yr) Source ID
26 Veneer dryers and heat 3 ZD 110 19.56
source (wood burner)
lbs/SF, (Softwood)
ES01-A
ES01-B
ES09
ES 10
30 Veneer dryers and heat 1 S S 1 19.40
source (wood burner)
lbs/SF, (Hardwood)
ES01-A
ES01-B
ES09
ES 10
Total: 38.97

Emissions by Operating Scenario
for
Xylene (mixed isomers)
2013 Inventory
Facility Name: Moncure Plywood
Facility ID: 1900039 Permit Number(s): 03424T23
Emission
Process Rate Emission
ID Operating Scenario 2. (Pounds/Yr) Source ID
26 Veneer dryers and heat 1 Co0 ^'12�j 110 84.30
source (wood burner)
lbs/SF, (Softwood)
ES01-A
ES01-B
ES09
ES10
30 Veneer dryers and heat 2 a , Z S y,., s b 33.04
source (wood burner)
lbs/SF, (Hardwood)
ES01-A
ES01-B
ES09
ES10
11 250 horsepower diesel- 0.02
fired water pump
IES19
35 250 HP Diesel Fired Water Pump#24ES23 0.01
IES 19
Total: 117.36

Boise Cascade -
Moncure Plywood Plant
NC DENR Raleigh Regional Office
Moncure Plywood LLC
306 Corinth Rd
P.O.Box 230
Moncure,NC 27559
(919)-542-2311
FAX[phone]
Certified Mail/Return:Receipt Request `� !
7012 3460 0002 13513321 I
June 26, 2014
Patrick Butler
Raleigh Regional Office
1628 Mail Service Center
Raleigh,NC 27699-1628
Per General Conditions 3.X of Title V Permit 03424T23, Moncure Plywood LLC submits our annual
Air Emissions Inventory for 2013.
If you have any questions or need additional information,please contact me at(803) 581-9261 or cell
at(803)374-3564.
Sine ly,
Brian Van Gelder
Project&Environmental Manager
Enclosures: (2)2013 North Carolina Air Emissions Inventories
Cc: Brian Van Gelder—Moncure Plywood LLC

Y
2013 NORTH CAROLINA NC DENR Raleigh Regional Ottice
AIR EMISSIONS INVENTORY
Prepared for:
Boise Cascade
Moncure Plywood
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. 31829585
June 2014

TABLE OF •
.Inventory Certification Letter A
Emission Source & Operating Scenario List B
List of Emission Sources & Control Devices C
Facility Summary D
Emission Source Operating Scenario Forms E
Supporting Data F
li
P:VOBS4\20MMONCURE PLYW00D\AE1\T0C.D0CX

h
I
I
Appendix A
Inventory Certification Letter
,P
a

Inventory Certification Form(Title V)
Facility Name: Moncure Plywood 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 2013
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).
STATEMENT:CERTIFICATION
(Important: Legally Responsible Official-read dsie"fter all submissions are fInal.)
I certify that I am the responsible official for this facility,as described above, and hereby certify that the information contained
in this air emissions report, including attached calculations and documentation, is true, accurate and complete. (Subject to legal
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 Signed:
Printed Name: Jeffrey Matuszak
Signature:
This form p/ o Title V facil' 'es. If this facility is not classified as Title V,please telephone your regional office Emission
Inventory contact at once for proper forms.
[e-mail]
Email address of Responsible Official: _
Information on this Form cannot be held confidential C DENR Raleigh Regional Once
133

i1
s-r
Appendix S
Emission Source & Operating Scenario List
i �
T

As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit : 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
Emission Source & Operating Scenario List — See Instructions
ES Group ID ES ID OS ID OS Description
GR2 I-10, I-9 32 Green Veneer Stackers
26 Veneer dryers and heat source(wood
burner)lbs/SF,(Softwood)
27 Veneer dryers and heat source(wood
ES01-13
G-24 ESO1—A, ES10, burner)HAPS lb/mmBtu, (Softwood)
1—B
>0 Veneer dryers and heat source(wood
burner) lbs/SF, (Hardwood)
31 Veneer dryers and heat source(wood
burner)HAPS lb/mmBtu,(Hardwood)
G-25 I-4,I-5 Ink and painting operations
G-27 ES14,ES17 20 Woodwaste Transfer(Rechipper)
system
ES-13-25HP NONE NONE
ES-13-40HP NONE NONE
ES-13—CC NONE NONE
ES-13—PO NONE NONE
ES-13—PS NONE NONE
ES03—CC NONE NONE
ES03—CS NONE NONE
ES03—PSS NONE NONE
ES03—SMS-1 21 Dry Waste transfer system
ES03—SMS-2 NONE NONE
ES03—SS NONE NONE
ESO4 12 wood sander
ES 12 17 dry wood residual storage silo
10 glue mixing,application and hot
ES 13—GMO presses operations(Hardwood)
28 glue mixing,application and hot
presses operations, (softwood)
ES 15 19 tongue and groove operations
ES 16 9 plywood hog
ES20 18 Vat Operations: Heating of Blocks
ES21 33 End Sealer Spray Booth
ES22 34 Tongue and Groove Saw
1-1 2 Bark hogging operations
3

I-11 25 Hammer hog truck dump—no controls
i I-12 24 Dry Waste truck dump
' I-2 3 Core chipping and handling operations
i
I-3 4 Green veneer hogging operations
I-6 6 Plywood surface patching
1-7 7 Maintenance parts washer
I-8 8 Veneer diverter exhaust cyclone
IES—GWS 16 Green wood fuel storage silo
11 250 horsepower diesel—fired water
IES 19 pump
35 250 HP Diesel Fired Water Pump
#2—IES23
i
_a
4

J
1
r �
i -
i
Appendix C
List of Emission Sources & Control Devices
__J

As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit: 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
Listing of Emission Sources and Control Devices on Permit. See instructions
ES ID on ES Description CS ID CS Description CD ID's
Air Permit
ES-13-25HP 25 panel hot press
ES-13-40HP 40 panel hot press
ES-13—CC Curtain coater
ES-13—PO Paper overlay operation
ES-13—PS Plywood spreader
Fluidized bed wood burner
with blending chamber and
ESO1—A dedicated overfire air fan(80.0 CS-1 multicyclone CD02
million Btu/hr heat input
capacity)
Boiler(29.79 million Btu/hr
ESO1—B heat input capacity,based on CS-1 multicyclone CD02
slipstream gas from ID No.
ES-01—A)(NSPS Subpart Dc)
ES03—CC Core composer with saw
ES03—CS Core saw(green or dry veneer)
ES03—PSS Panel sawing system
ES03—SMS-1 String machine including saws CS-3 bagfilter(7,095 square feet of filter CD03—WWTC,CD06
area),dry waste transfer cyclone
ES03—SMS-2 String machine including saws
ES03—SS Strip saw
Bagfilter(6,200 square feet of filter
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 Direct wood—fired veneer dryer CS-1 multicyclone CD02
ES10 M72 t wood—fired veneer dryer CS-1 multicyclone CD02
ES12 Dry wood residual storage silo CS-5 cartridge filter(1,800 square feet of CD21
filter area)
Glue mixing operations
ES 13—GMO consisting of two resin storage
tanks and four mixed glue
tanks
ES14 Rechip blow hog(green wood CS-12 Cyclone(60 inches in CD18,CD03—WWTC,
1

only) diameter),Woodwaste transfer cyclone CD06
(154 inches in diameter),Bagfilter
(7,095 square feet of filter area),
ES 15 tongue and groove operations
ES 16 Plywood waste hog CS-3 bagfilter(7,095 square feet of filter CD03—WWTC,CD06
area),dry waste transfer cyclone
(60 inches in
l c C
Y
Green wood sizing operations ES17 including sizing screens and CS-12 diameter)Woodwaste transfer cyclone CD18'CD03—WWTC,
bins (154 inches in diameter),Bagfilter CD06
(7,095 square feet of filter area),
ES20 Vat operations
ES21 End sealer spray booth
ES22 Tongue and groove saw CS-7 bagfilter(7,095 square feet of filter CD06
(plywood finishing) area)
I-1 Bark hogging operations with
I
two saws
I-10 green wood veneer stacker No.
2
I-11 hammer hog truck dump
I-12 dry waste truck dump
I-2 Core chipping and handling
I-3 Green veneer hogging
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
I-9 green wood veneer stacker No.
j 1
IES—GWS Green wood fuel storage silo
j Diesel—fired water pump(250
IES 19 Horsepower maximum power
output) for emergency purposes
only
i
2

1
t �
I �I
Appendix D
Facility Summary

Facility Total CY 2013 Emissions Summary
As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit : 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory-Calendar Year 2013
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 2013 2012 % Change
Criteria Pollutants
Actual Emissions Tons/Year
Pollutant CAS 2013 2012 % Change
CO CO 29.28 27.29 7.292047%
NOx NOx 44.14 38.94 13.35388%
PM TSP TSP 66.42 57.64 15.232475%
PM 10 PM 10 66.4 57.64 15.197783%
PM2.5 PM2.5 55.2 52.93 4.288684%
S02 S02 0.7 3.55 -80.28169%
VOC VOC 63.3 51.77 22.271584%
Hazardous Air Pollutants HAPS and/or Toxic Air Pollutants TAPS
Actual Emissions Pounds/Year
Pollutant I CAS 1 2013 1 2012 % Change
Pollutant Grou :Antimon Compounds total mass, inc elemental SB Group Sum:0.0
Antimony Unlisted Compounds (Specify SBC-Other 0.0 2.24355_T -100.0%
Component of SBC
Pollutant Group:Arsenic Compounds (total mass of elemental AS,arsine and all inorganic compounds) Group
Sum:1.39462
Arsenic Unlisted Compounds ( Specify ASC-Other 1.39462 .21016 563.5991%
Component of ASC
Pollutant Group:Beryllium compounds Total mass Group Sum:0.0
Beryllium Compound,Unlisted (Specify BEC-Other 0.0 Not reported N/A
Component of BEC
Beryllium metal (unreacted) (Component of 7440-41-7 0.0 .31239 -100.0%
BEC
Pollutant Grou :Cadmium compounds total mass inc elemental metal Group Sum:2.06161
Cadmium Metal (elemental unreacted, 7440-43-9 2.06161 7.51694 -72.57381%
Component of CDC
Cadmium Unlisted Compounds (Specify CDC-Other 0.0 Not reported N/A
Component of CDC
71

1 N,
Pollutant Group:Chlorinated Dioxin Co m ounds of interest as HAP or TAP GroupSum:.69298
Hexachlorodibenzo-p-dioxin 1,2,3,6,7,8 57653-85-7 0.69298 Not reported N/A
(Component of CLDC
Pollutant Grou :Chromium I Soluble Chromate Compounds (Component of CRC Group Sum:3.01879
Chromic acid(VI) (Component of So1CR6 7738-94-5 3.01879 .99398 203.70732%
CRC
Pollutant Grou :Chromium-All/Total Inc Chromium VI categories,metal and Others Group Sum:13.41348
Chromic acid(VI) (Component of SolCR6
CRC 7738-94-5 3.01879 .99398 203.70732%
Chromium Unlisted Compounds (Specify CRC-Other 10.39469 4.96989 109.153305%
Component of CRC
Pollutant Group:Cobalt compounds Grou Sum:0.0
Cobalt Unlisted Compound(Specify COC-Other 0.0 1.84596 -100.0%
Component of COC
- Pollutant Grou :Lead and Lead com ounds G oup Sum:6.66993
Lead Unlisted Compounds (Specify and PBC-Other 6.66993 13.63171 -51.07048%
Component of PBC
-- Pollutant Grou :Man anese compounds Group Sum:1078.44888
Manganese Unlisted Compounds (Specify MNC-Other 1078.4489 454.3904 137.3397%
Component of MNC
Pollutant Grou :Mercu Compounds-all total mass inc Hg Va or Group Sum:.49808
Mercury Unlisted Compounds (Specify HGC-Other 0.0 Not reported N/A
Component of HGC
Mercury,vapor(Component of HGC 7439-97-6 0.49808 .99398 -49.89034%
Pollutant Grou :Nickel Compounds,sum total mass,inc elemental Grou Sum:5.06741
Nickel Unlisted Compounds (Specify Component of NIC) NIC-Other 0.0 Not reported N/A
Nickel metal(Component of NIC 7440-02-0 5.06741 9.3718 -45.929176%
Pollutant Grou :Pol c clic Organic Matter 7 PAH Compounds for NIF Group Sum:0.0
Benzo(a)pyrene(Component of POMTV 50-32-8 0.0 .7384 7-1
00.0%
POM7
Pollutant Grou :Pol c clic Organic Matter(Specific Compounds from OA PS for TV Group Sum:3.52816
Benzo(a)pyrene(Component of POMTV 50-32-8 0.0 .7384 -100.0%
POM7
Naphthalene(Component of POMTV 91-20-3 3.52816 27.54979 -87.19351%
Acetaldehyde 75-07-0 2352.3203 5051.53818 -53.433582%
Acrolein 107-02-8 342.27924 371.03699 -7.750643%
Benzene 71-43-2 182.10374 216.52572 -15.89741%
Butadiene, 1,3- 106-99-0 0.0 Not reported N/A
Carbon tetrachloride 56-23-5 1.10444 12.77973 -91.35788%
Chlorine 7782-50-5 342.15848 224.35526 52.50745%
Chlorobenzene 108-90-7 0.0 9.3718 -100.0%
Chloroform 67-66-3 0.0 7.95183 -100.0%
Cumene 98-82-8 1499.6632 2097.913 -28.516428%
Eth 1 benzene 100-41-4 0.0 8.80382 -100.0%
Ethyl chloride chloroethane 75-00-3 24.89575 55.38615 -55.050587%
Ethylene dichloride 1,2-dichloroethane 107-06-2 38.17047 86.01755 -55.624783%
Fluorides sum of all fluoride compounds) 16984-48-8 0.0 Not reported N/A
Formaldehyde 50-00-0 2354.128 2280.33298 3.2361467%
Hydrogen chloride(hydrochloric acid 7647-01-0 149.85675 159.03664 -5.772183%
72

1
Methanol 67-56-1 8461.967 11960.9429 —29.25335%
Methyl bromide 74-83-9 59.22956 83.7033 —29.23868%
Methyl chloride 74-87-3 11.52078 6.53186 76.37824%
Methyl ethyl ketone 78-93-3 121.89227 318.78475 —61.763454%
Methyl isobutyl ketone 108-10-1 184.86906 645.56895 —71.36339%
Methylene chloride 75-09-2 53.06976 74.7271 —28.981905%
_ Phenol 108-95-2 1741.9989 1476.73 17.963264%
Phosphorus Metal Yellow or White 7723-14-0 2360.4604 7.66784 30683.904%
Polycyclic Organic Matter(Inc PAH,
dioxins, etc.NC AP 42 historic amorphous POM 9.6722 35.50395 —72.75739%
lob
Pro ionaldeh de 123-38-6 79.18664 232.9338 —66.004654%
Selenium Compounds SEC 0.0 .79519 —100.0%
Styrene 100-42-5 0.0 152.0647 —100.0%
Toluene 108-88-3 0.0 320.83435 —100.0%
Trichlorobenzene, 1,2,4— 120-82-1 113.25191 160.2818 —29.342005%
Trichloroethane, 1,1,2— 79-00-5 0.0 Not reported N/A
Trichloroeth lene 79-01-6 0.0 8.51982 —100.0%
Vinyl chloride 75-01-4 38.96717 54.69188 —28.75145%
Vin lidene chloride 75-35-4 58.64297 Not reported N/A
X lene 1330-20-7 117.35508 338.85113 —65.366776%
X lene,o— 1 95-47-6 1 0.0 1 Not reported I N/A
73

Boise Cascade-Moncure Plywood
Facility-Wide Summary of Actual Emissions
2013 Air Emissions Inventory
URS Project No.31829585
FBB& Dry Waste Sander r.Veneer Hammer Hog Dry Waste
Compound Dryers Storage System Stackers Truck Dump Truck Dump Emissions Emissions
t ES-1910 ES-12 ES-l14 S-IN-9&10 IS-IN-11 IS-IN-12 Ib/ r tons/ r
CO 29.24 58,555 29.28
Ox 43.96 88,283 44.14
PM 33.50 0.60 0.22 0.61 0.00 0.00 132,860 66.43
PMIO 33.50 0.60 0.22 0.61 0.00 0.00 132,799 66.40
PM2.5 32.83 0.60 0.22 0.00 0.00 110,422 55.21
VOC 45.51 2.95 126,640 1 63.32
S02 0.69 1,401 0.70
Compound Emissions DeMinimus Report in
(lb/yr) Ib/yr (tb/yr) AEI?
Acetaldehyde T 1519.28 61).03, 2,352.32 10 Yes
Aceto henone H 0.80 0.80 100 No
Acrolein 342.27 342.28 10 Yes
Antimony&Compounds 1.50 1.50 10 No
Arsenic&Compounds T 1.39 1 1.39 0.01 Yes
Benzene T 182.05 182.12 1 Yes
Benzo a ene T 0.01 0.01 1 No
Beryllium Compounds 0.02 0.02 1 No
Cadmium Compounds 2.06 2.06 0.1 Yes
Carbon tetrachloride 1.10 1.10 1 Yes
Chlorine T 342.16 342.16 100 1 Yes
Chlorobenzene T 7.19 1 7.19 10 No
Chloroform T 1.10 1.10 100 No
Chromium-Other compds 10.39 10.39 0.1 Yes
Chromium VI Compounds(TM 3.02 3.02 0.01 Yes
Cobalt compounds H 0.92 0.92 1 No
Cumene 1499.24 1,499.24 100 Yes
Dinitro henol,2,4- 0.06 0.06 0.1 No
Di 2-eth lhex I hthalate DEHP T 0.02 0.02 10 No
Ethyl benzene 13.56 13.56 100 No
Ethyl chloride chloroethane 24.86 24.86 10 Yes
Ethylene dichloride 38.12 38.12 1 Yes
Formaldehyde T 1949.08 .` 2,354.13 10 Yes
Hexachlorodibenzo- oxin 1,2,3,6,7,8 0.69 0.69 0.00001 Yes
Hydrogen chloride T 149.86 149.86 1 100 Yes
Lead and Lead compounds 6.67 6.67 1 Yes
Manganese&compounds T 1078.45 1,078.45 10 Yes
Mercury Compound 0.50 0.50 0.001 Yes
Methanol 2655.42 1O L47 8,461.97 1000 Yes
Methyl bromide 59.20 1 59.20 1 Yes
Meth 1 chloride 11.52 11.52 1 Yes
Methyl chloroform TH 17.02 17.02 100 No
Methyl ethyl ketone T 85.08 121.68 100 Yes
Methyl Isobutyl Ketone 148.00 184.83 10 Yes
Methylene di hen l diisoc ante MDI)(H) 0.00 10 No
Methylene chloride 53.02 53.02 1 Yes
Naphthalene 3.52 1 3.53 1 Yes
Nickel Compounds T 5.07 5.07 1 Yes
Nitro phenol,4- 0.04 0.04 1 10 No
Pentachloro henol T 0.02 0.02 1 No
Perchloroeth lene T 10.65 10.65 100 No
Phenol 290.25 1,742.21 100 Yes
Phosphorus Metal,Yellow or White H 2360.46 2,360.46 1 Yes
Polychlorinated bi hen is TH 0.00 0.00 10 No
Pol c clic Organic Matter 9.66 9.67 1 Yes
Pro ionldeh de 79.14 79.14 10 Yes
Propylene dichloride 7.28 7.28 10 No
Selenium compounds 0.23 0.23 10 No
Styrene TH 34.70 34.70 100 No
Tetachlorodibenzo- ioxin,2,3,7,8- T 0.00 0.00 0.00001 No
Toluene T 29.18 29.21 100 No
Trichlorobenzene,1,2,4 113.31 113.31 100 Yes
Trichloroeth lene T 8.62 8.62 1000 No
Trichlorofluoromethane CFC I I I T 6.89 6.89 100 No
Trichloro henol,2,4,6- 0.12 0.12 1 No
Vinyl acetate 7.37 100 No
Vin l chloride(T 39.00 39.00 0.1 Yes
Vin lidenechloride 1,1-dichloroethene T 58.68 58.68 0.1 Yes
X lene(TH) 117.29 117.31 100 Yes

Appendix E
Emission Source Operating Scenario Forms

As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit : 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2013
1. Emission Source ID(from permit)or Group G-24 consisting of ESO1—A,ES09, ES10, ES01-13
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 2013: 45078000 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 dryer erp
09B VERTICAL STACK 66 1 370 100 4712.38 Veneer dryer e
09C VERTICAL STACK 66 1 340 150 7068.58 Veneer dryer erp
09cool VERTICAL STACK 46 4 107 35 26389.37 Veneer drver ery
10A VERTICAL STACK 66 1 350 155 7304.2 Veneer dryer erp
lOB VERTICAL STACK 66 1 370 100 4712.38 Veneer dryer erp
IOC VERTICAL STACK 66 1 340 150 7068.58 Veneer dryer erp
IOcool VERTICAL STACK 46 4 105 35 26389.37 Veneer dryer erp
7

Operating Scenario: OS-26 Emission Source/Group ID: G-24
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
j 11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an +Dec 25% 25% une-Aug. 25% FSept.-Nov. 25%
013 �arch-May
13 013 13
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
a
tia Emissions- Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
1 2013
t
Emissions- Emission Control
i_ Criteria Pollutant Criteria Estimation Efficiency Emission
��QS) Code Pollutants Method Code (Net after Factor Ef Control
-� Pollutants
(Tons/Year) (See Instructions) all controls)
2013
CO CO 13.52 04 0 0.0006 AFTER
t NOx NOx 08 _ 0
TSP TSP 08 65
PM10 PM10 08 65
PM2.5 PM2.5 08 65
S02 S02 08 0
VOC VOC 39.89 04 0 0.00177 AFTER
i-- HAP/TAP Emissions
Emission Control Emission CAS Estimation Efficiency
Pollutants (In Alphabetical (see instructions) HAP/TAPS Method Code (Net after all Factor EF Control
Order) (Pounds/Year)
See Instructions controls)
2013
' Acetaldehyde 75-07-0 1081.872 08 0 0.000024 AFTER
Acrolein 107-02-8 306.5304 08 0 0.0000068 AFTER
Benzene 71-43-2 157.773 08 0 0.0000035 AFTER
Cumene 98-82-8 752.8026 08 0 0.0000167 AFTER
Ethyl chloride 75-00-3 4.82335 08 0 1.07E-7 AFTER
chloroethane
Ethylene dichloride
:�? 1,2-dichloroethane 107-06-2 7.39279 08 0 1.64E-7 AFTER
Formaldehyde 50-00-0 1126.95 04 0 0.000025 AFTER
'+ Methanol 67-56-1 1861.7214 08 0 0.0000413 AFTER
Methyl bromide 74-83-9 29.7064 08 0 6.59E-7 AFTER
Methylene chloride 75-09-2 26.6411 08 0 5.91 E-7 AFTER
Phenol 108-95-2 153.71598 08 0 0.00000341 AFTER
-' Trichlorobenzene, 12,4- 120-82-1 56.79828 08 0 0.00000126 AFTER
9

Vinyl chloride 75-01-4 19.56385 08 0 4.34E-7 AFTER
Vin lidene chloride 75-35-4 28.53437 08 0 633E-7 AFTER
X lene 1330-20-7 84.29586 08 0 0.00000187 AFTER
=�k
i
� I
_j
Cl
G
P
i
v
I
1
L
' I
I
v
10

As entered in AFRO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit : 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2013
1. Emission Source ID(from permit)or Group G-24 consisting of ES01—A, ES09, ES10,ES01-13
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 ib/mmBtu,
(Softwood)
4. SCC Number/Description: 30700740/Plywood Operations ; Direct Wood—Fired Dryer: Non—specified
Pine Species Veneer
5. Throughput/units in 2013: 151685 E6BTU/yr
(e.g. production or fuel use):
6. Fuel Information (If fuel is used) % Sulfur —To
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 tines):
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 e
09B VERTICAL STACK 66 1 370 100 4712.38 Veneer dryer erp
09C VERTICAL STACK 66 1 340 150 7068.58 Veneer dryer erp
09cool VERTICAL STACK 46 4 107 35 26389.37 Veneer dryer erp
10A IVERTICAL STACK 66 1 350 155 7304.2 Veneer dryer erp
10B IVERTICAL STACK 66 1 370 100 4712.38 Veneer dryer e
10C IVERTICAL STACK 1 66 1 1 340 150 7068.58 Veneer dryer erp
11

i
Operating Scenario: OS - 30 Emission Source/Group ID: G-24
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
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 1013
une-Aug. o ept.-Nov. o
013 25/6 �arch-May
13 25 /° 25/0 013 25/0
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 y Ef Control
Pollutants Method Code (Net after Factor
(Tons/Year) See Instructions all controls
2013
Criteria Emissions- Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po�QS Code Pollutants Method Code (Net after Factor Ef Control
Pollutantss (Tons/Year) (See Instructions) all controls)
2013
CO CO 15.72 04 0 0.000376 AFTER
NOx NOx 08 0
TSP TSP 08 65
PM10 PM10 08 65
PM2.5 PM2.5 08 65
S02 S02 08 0
VOC VOC 5.6 04 0 0.000134 AFTER
HAP/TAP Emissions Emission Control
Pollutants (In Alphabetical CAS HAP/,TAPS Estimation Efficiency Emission EF Control
Order) (see instructions) (Pounds/Year) Method Code (Net after all Factor
See Instructions controls)
2013
Acetaldehyde 75-07-0 437.41105 08 0 0.00000523 AFTER
Benzene 71-43-2 24.25415 08 0 2.9E-7 AFTER
Cumene 98-82-8 746.86055 08 0 0.00000893 AFTER
Ethyl chloride 75-00-3 20.0724 08 0 2.4E-7 AFTER
chloroethane
Ethylene dichloride 107-06-2 30.77768 08 0 3.68E-7 AFTER
12-dichloroethane
Formaldehyde 50-00-0 822.13205 04 0 0.00000983 AFTER
Methanol 67-56-1 793.69615 08 0 0.00000949 AFTER
Methyl bromide 74-83-9 29.52316 08 0 3.53E-7 AFTER
Methyl ethyl ketone 78-93-3 84.47135 08 0 0.00000101 AFTER
Methyl isobutyl ketone 108-10-1 80.54051 08 0 9.63E-7 AFTER
j Methylene chloride 75-09-2 26.42866 08 0 3.16E-7 AFTER
Phenol 1 108-95-2 136.32505 08 0 0.00000163 AFTER
17

Chromium Unlisted Compounds
{{ (Specify Component of CRC
?t_ Hexachlorodibenzo—p—dioxin 1,2,3,6,7,8
(Component of CLDC 57653-85-7 0.45028 08 0 0.0000016 AFTER
Hydrogen chloride(hydrochloric acid 7647-01-0 97.37374 08 0 0.000346 AFTER
Lead Unlisted Compounds(Specify and
Component of PBC) PBC—Other 4.33398 08 0 0.0000154 AFTER
Manganese Unlisted Compounds MNC—Other 700.75323 08 0 0.00249 AFTER
' (Specify Component of MNC
Mercury,vapor(Component of HGC 7439-97-6 0.32364 08 0 0.00000115 AFTER
Methyl chloride 74-87-3 7.48596 08 0 0.0000266 AFTER
Naphthalene(Component of POMT 91-20-3 2.288 08 0 0.00000813 AFTER
Nickel metal(Component of NIC 7440-02-0 3.2927 08 0 0.0000117 AFTER
Phosphorus Metal Yellow or White 7723-14-0 1533.77715 08 0 0.00545 AFTER
Polycyclic Organic Matter(Inc PAR,
dioxins,etc.NC AP 42 historic POM 6.27582 08 0 0.0000223 AFTER
amorphous lob
'e
22

Boise Cascade-Moncure Plywood
Emission Source(s): Fluidized Bed Wood Boiler and Two Direct Heated Dryers
Source ID Number(s): ES-01,ES-09,ES-10,CD-02(multiclone on boiler)
Emission Point(s): EP-09a-d,EP-10a-d
2013 Actual Process Throughput: 8,064 Boiler operating hours/yr
37,465 ton wood/yr
433,111 MMBtu/yr
224,093 MMBtu/yr Green Wood
209,019 MMBtu/yr Dry Wood
83,635,000 sf/yr Hardwood
45,078,000 sf/yr Softwood
128,713,000 sf/yr Total Plywood Production J
281,427 MMBtu/yr Hardwood V� n(
151,685 MMBtu/yr Softwood n�� C� �V
Actual Emissions Summary: d
Hardwood Softwood Total
Emissions*
Compound Emission Factor Units Ref. Emission Factor Units Ref. Emissions* Emissions
ton/ r ton/ r ton/ r
CO 3.76E-04 lb/sf 1 15.72 6.00E-04 lb/sf 1 13.52 29.2
NOx 2.03E-01 lb/MMBtu 6 28.56 ✓ 2.03E-01 lb/MMBtu 6 15.40 44.0
PM 8.308 lb/hr 3 21.77 ✓ 8.308 lb/hr 3 11.73 -_ 33.5
PM 10 8.308 lb/hr 3 21.77 ✓ 8.308 lb/hr 3 11.73 - 33.5
PM2.5 8.14 lb/hr 3 21.33 ✓ 8.14 lb/hr 3 11.50 - 32.8
VOC as acetic acid-hardwood and pinene-softwood) 2.41 E-04 Ib/sf 1 10.09 1.07E-03 lb/sf 1 24.12 34.2
WPPI VOC 1.34E-04 lb/sf 4 5.62 ✓ 1.77E-03 lb/sf 4 39.89 45.5
SO2 3.18E-03 lb/MMBtu 6 0.45 3.18E-03 lb/MMBtu 6 0.24 - 0.69
Emissions*
Compound Emission Factor Units Ref. Emissions*
r Emission Factor Units Ref. Emissions* Emissions
lb/ r Ib/ r
Acetaldehyde(TH) 5.23E-06 Ib/sf 2 437.41 2.40E-05 lb/sf 2 1081.87 1519.28
Aceto henone(H) 1.84E-06 lb/MMBtu 6 0.52 1.84E-06 lb/MMBtu 6 0.28 0.80
Acrolein(TH) 1.27E-04 lb/MMBtu- 6 35.74 6.80E-06 lb/sf 2 306.53 342.27
Antimony&compounds (H) 3.46E-06 lb/MMBtu 6 0.97 3.46E-06 lb/MMBtu 6 0.52 1.50
Arsenic&compounds (TH) 3.22E-06 lb/MMBtu 6 0.91 3.22E-06 lb/MMBtu 6 0.49 - 1.39
Benzene(TH) 2.90E-07 lb/sf 2,7 24.28 3.50E-06 Ib/sf 2 157.77 182.05
Benzo(a) ene (T) 1.52E-08 lb/MMBtu 6 0.00 1.52E-08 lb/MMBtu 6 0.00 0.01
Beryllium&compounds(TH) 4.00E-08 lb/MMBtu 6 0.01 4.00E-08 lb/MMBtu 6 0.01 0.02
Cadmium&compounds(TH) 4.76E-06 lb/MMBtu 6 1.34 4.76E-06 lb/MMBtu 6 0.72 - 2.06
Carbon tetrachloride(TH) 2.55E-06 lb/MMBtu 6 0.72 2.55E-06 lb/MMBtu 6 0.39 1.10
Chlorine(TH) 7.90E-04 lb/MMBtu 5 222.33 7.90E-04 lb/MMBtu 5 119.83 - 342.16
Chlorobenzene(TH) 1.66E-05 lb/MMBtu 6 4.67 1.66E-05 lb/MMBtu 6 2.52 7.19

Boise Cascade-Moncure Plywood
Emission Source(s): Fluidized Bed Wood Boiler and Two Direct Heated Dryers
Source ID Number(s):ES-01,ES-09,ES-10,CD-02(multiclone on boiler)
Emission Point(s): EP-09a-d,EP-10a-d
2013 Actual Process Throughput: 8,064 Boiler operating hours/yr
37,465 ton wood/yr
433,111 MMBtu/yr
224,093 MMBtu/yr Green Wood
209,019 MMBtu/yr Dry Wood
83,635,000 sf/yr Hardwood
45,078,000 sf/yr Softwood
128,713,000 sf/yr Total Plywood Production
281,427 MMBtu/yr Hardwood
151,685 MMBtu/yr Softwood
Actual Emissions Summar.:
Hardwood Softwood Total
Compound Emission Factor Units Ref. Ib! r Emissions* Emission Factor Units Ref. Emissions* Emissions*
Ib! r Ib/ r
Chloroform TH 2.55E-06 lb/MMBtu 6 0.72 2.55E-06 lb/MMBtu 6 0.39 1.10
Chromium compounds H 2.40E-05 lb/MMBtu 6 6.75 2.40E-05 lb/MMBtu 6 3.64 10.39
Chromium VI T/H 6.97E-06 lb/MMBtu 6 1.96 6.97E-06 lb/MMBtu 6 1.06 3.02
Cobalt compounds H 2.12E-06 lb/MMBtu 6 0.60 2.12E-06 lb/MMBtu 6 0.32 0.92
Cumene H 8.93E-06 lb/sf 2,7 746.44 1.67E-05 lb/sf 2,7 752.80 1499.24
Dinitro henol,2,4- H 1.31E-07 lb/MMBtu 6 0.04 •1.31 E-07 lb/MMBtu 6 0.02 0.057
Di 2-eth lhex 1 hthalate DEHP TH 4.65E-08 lb/MMBtu 6 0.01 4.65E-08 lb/MMBtu 6 0.01 0.020
Ethyl benzene H 3.13E-05 lb/MMBtu 6 8.81 3.13E-05 lb/MMBtu 6 4.75 13.56
Ethyl chloride chloroedme H 2.40E-07 lb/sf 2,7 20.05 1.07E-07 lb/sf 2,7 4.81 24.86
Ethylene dichloride 1,2-dichloroethane TH 3.68E-07 lb/sf 2,7 30.74 1.64E-07 lb/sf 2,7 7.38 38.12
Formaldehyde TH 9.83E-06 lb/sf 1 822.13 2.50E-05 lb/sf 1 1126.95 1949.08
Hexachlorodibenzo- Toxin 1,2,3,6,7,8 T 1.60E-06 lb/MMBtu 5 0.45 1.60E-06 lb/MMBtu 5 0.24 - 0.69
Hydrogen chloride(hydrochloric acid TH 3.46E-04 lb/MMBtu 6 97.37 3.46E-04 lb/MMBtu 6 52.48 - 149.86
Lead&compounds H 1.54E-05 lb/MMBtu 6 4.33 1.54E-05 lb/MMBtu 6 2.34 6.67
Manganese&compounds TH 2.49E-03 lb/MMBtu 6 700.75 2.49E-03 lb/MMBtu 6 377.69- 1078.45
Mercury,vapor Include in Merc &Com TH 1.15E-06 lb/MMBtu 6 0.32 1.15E-06 lb/MMBtu 6 0.17 - 0.50
Methanol H 9.49E-06 lb/sf 2 793.70 4.13E-05 lb/sf 2 1861.72 2655.42
Methyl bromide H bromomethane) 3.53E-07 lb/sf 2,7 29.50 6.59E-07 lb/sf 2,7 29.70 ✓ 59.20
Methyl chloride H chloromedme 2.66E-05 lb/MMBtu 6 7.49 2.66E-05 ih/MMBtu 6 4.03 11.52
Methyl chloroform(TH)(1,1,1 trichloroethane 3.93E-05 lb/MMBtu 6 11.06 3.93E-05 lb/MMBtu 6 5.96 17.02
Meth 1 ethyl ketone TH 1.01 E-06 lb/sf 2,7 84.26 5.39E-06 lb/MMBtu 6 0.82 - 85.08
Methyl isobutyl ketone TH 9.63E-07 Ib/sf 2,7 80.50 4.45E-04 lb/MMBtu 6 67.50 148.00
Methylene chloride(TH)(dichloromethane 3.16E-07 lb/sf 2,7 26.39 5.91 E-07 lb/sf 2,7 26.63 53.02
hthalene H 8.13E-06 lh/MMBtu 6 2.29 8.13E-06 lb/MMBtu 6 1.23 "' 3.52
Nickel metal(Component of Nickel&Compounds) TH 1.17E-05 lb/MMBtu 6 3.29 1.17E-05 lb/MMBtu 6 1.77 1 5.0711
Nitro henol,4- H 9.41E-08 lb/MMBtu 6 0.03 9.41E-08 lb/MMBtu 6 0.01 0.041
Pentachloro henol TH 4.48E-08 lb/MMBtu 6 1 0.01 4.48E-08 lb/MMBtu 6 0.01 0.019

Boise Cascade-Moncure Plywood
Emission Source(s): Fluidized Bed Wood Boiler and Two Direct Heated Dryers
Source ID Number(s):ES-01,ES-09,ES-10,CD-02(multiclone on boiler)
Emission Point(s): EP-09a-d,EP-10a-d
2013 Actual Process Throughput: 8,064 Boiler operating hours/yr
37,465 ton wood/yr
433,111 MMBtu/yr
224,093 MMBtu/yr Green Wood
209,019 MMBtu/yr Dry Wood
83,635,000 sf/yr Hardwood
45,078,000 sf/yr Softwood
128,713,000 sf/yr Total Plywood Production
281,427 MMBtu/yr Hardwood
151,685 MMBtu/yr Softwood
Actual Emissions Summary:
Hardwood Softwood Total
Compound Emission Factor Units Ref. Ib/ r Emissions* Emission Factor Units Ref. Emissions* Emissions*
Ib/ r Ib/ r
Perchloroeth lene PERC tetrachloroeth lene TH 2.46E-05 lb/MMBtu 6 6.92 2.46E-05 lb/MMBtu 6 3.73 10.65
Phenol TH 1.63E-06 Ib/sf 2,7 136.53 3.41E-06 Ib/sf 2 153.72 290.25
Phosphorus Metal,Yellow or White H 5.45E-03 Ib/MMBtu 6 1533.78 5.45E-03 lb/MMBtu 6 826.68- 2360.46
Polychlorinated bi hen is TH 8.15E-09 lb/MMBtu 5 0.00 8.15E-09 lb/MMBtu 5 0.00 0.004
Pol c chc Organic Matter H 2.23E-05 lb/MMBtu 6 6.28 2.23E-05 lb/MMBtu 2 3.38 9.66
Pr ionaldeh de H 9.08E-07 lb/sf 2,7 75.90 2.14E-05 lb/MMBtu 6 3.25 79.14
Propylene dichloride H 1,2 dichloro a 1.68E-05 lb/MMBtu 6 4.73 1.68E-05 lb/MMBtu 6 2.55 7.28
Selenium compounds H 5.39E-07 lb/MMBtu 6 0.15 5.39E-07 lb/MMBtu 6 0.08 0.23
Styrene TH 3.87E-07 lb/sf 2,7 32.37 1.54E-05 lb/MMBtu 6 2.34 34.70
Tetrachlorodibenzo- -dioxin,2,3,7,8- (TH) 8.60E-12 lb/MMBtu 5 0.00 8.60E-12 lb/MMBtu 5 0.00 3.72E-06
Toluene TH 3.42E-07 Ib/sf 2,7 28.62 3.67E-06 lb/MMBtu 6 0.56 29.18
richlorobenzene,1,2,4- H 6.75E-07 Ib/sf 2,7 56.45 1.26E-06 Ib/sf 2,7 56.85 113.31
richloroeth lene TH 1.99E-05 lb/MMBtu 6 5.60 1.99E-05 lb/MMBtu 6 3.02 8.62
richlorofluoromethane CFC I 1 l T 1.59E-05 lb/MMBtu 6 4.47 1.59E-05 lb/MMBtu 6 2.41 6.89
Trichloro henol,2,4,6- H 2.76E-07 lb/MMBtu 6 0.08 2.76E-07 lb/MMBtu 6 0.04 0.120
Vinyl chloride chloroethene)(TH) 2.32E-07 lb/sf 2,7 19.42 4.34E-07 lb/sf 217 19.58 39.00
Vin hdene chloride 1,1-dichloroethene) TH 3.60E-07 I Ib/sf 2,7 30.13 6.33E-07 lb/sf 1 2,7 28.55 58.68
X lene(TH) 3.95E-07 lb/sf 2,7 32.99 1.87E-06 lb/sf 2 84.30 117.29
*Note: All emissions include emissions from wood combustion and wood drying.
References:
1-Stack Testing Data, 1996
2-NCASI Wood Products Database,Updated 2013,Direct Fired Veneer Dryer
3-Based on Feb. 12,2010 stack test. PM 10 assumed to be equal to PM. PM2.5 assumed to be 98%
4-OTM26:hiterim VOC Measurement Protocol for the Wood Products Industry-July 2007
5-AP-42 Section 1.6,September 2006
6-Tables 4.1,4.3,4.5,5.1 of NCASI TB 1013,March 2013,median values(metal factors with mechanical collector,for multiclone).
7-Half the average detection values are used for non-detects.

As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit : 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2013
1. Emission Source ID(from permit)or ES03—SMS-1
Emission Source Group ID
2. Emission Source Description: Woodworking operations consisting of three string machine saws,a core saw, a
strip saw,a panel sawing system and a core composer, saw,sander baghouse
(ID No. CD-05)
3. Operating Scenario ID/Description: OS—21/Dry Waste transfer system
4. SCC Number/Description: 30700710/Plywood Operations ; Sawing
5. Throughputtunits in 2013: 128713000 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-3 CD03—WWTC Woodwaste transfer cyclone 154 inches in diameter
CS-3 CD06 Ba filter(7,095 square feet of filter area
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
erp for dry waste
erp-08 VERTICAL STACK 51 3.5 80 55 31749.72 transfer cyclone and
bagfilter
27

r`7
Operating Scenario: OS—21 Emission Source/Group ID:
ES03—SMS-1
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
r Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
I
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
' an—Feb +Dec o o une—Aug. o Sept.—Nov. o
013 25/0 �arch—May
13 25/0 �013 25/0 013 25/o
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2013
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
o� Code Pollutants Method Code Ef Control
Pollutants an (Net after Factor
(Tons/Year) (See Instructions) all controls)
2013
CO CO 08 0
NOx NOx 08 0
TSP TSP 15.35 04 85 AFTER
PM10 PM10 15.35 04 85 AFTER
PM2.5 PM2.5 15.35 04 0 AFTER
S02 S02 08 0
VOC VOC 08 0
HAP/TAP CAS Emissions Emission Control
Pollutants (In HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) See Instructions) (Net after all controls)
-� 2013
28

' 1
Boise Cascade-Moncure Plywood
Emission Source: Dry Waste Transfer System
Source ID Number: ES-03,CD-06
Emission Point: EP-06
2013 Actual Process Throughput:
j Hardwood Plywood Production 83,635,000 sf/yr
Softwood Plywood Production 45,078,000 sf/yr
Emissions Summary:
/
Softwood Hardwood
CompoundT Emission Factor Ref. Emission Factor Ref. Emissions
M 6.60E-04lb/sf 1 1.15E-05lb/sf 1 15.35 tpy
—' M-10 6.60E-04lb/sf 1 1.15E-05lb/sf 1 15.35 tpy
M-2.5 6.60E-04 lb/sf 1 1.15E-05 lb/sf 1 1 15.35 y
References:
1. Emission factor from original Title V Permit Application

As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit : 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2013
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 2013: 39000000 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—W WTC Woodwaste transfer cyclone 154 inches in diameter
3 CS-10 CD06 Ba Ilter(7,095 square feet of filter area
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ent lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP
(in feet) Circle(enter#): (F) (Feet/see) 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
29

Operating Scenario: OS— 12 Emission Source/Group ID: ESO4
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% 25"�o me—Aug. 25"�o �013
ept.—Nov. 25%
013 �arch—May
13 013
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG GHG Estimation Efficiency Emission
Pollutants CAS Pollutants Method Code (Net after Factor Ef Control
Tons/Year See Instructions) all controls
2013
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
��QS) Code Pollutants Method Code (Net after Factor
Ef Control
Pollutants (Tons/Year) (See Instructions) all controls)
�- 2013
CO CO 08 0
NOx NOx 08 0
TSP TSP 0.22 04 95 AFTER
PM10 PM10 0.22 04 95 AFTER
PM2.5 PM2.5 0.22 04 95 AFTER
S02 S02 08 0
VOC VOC 2.95 08 0
HAP/TAP Emissions Emission Control
CAS Estimation Efficiency Emission
Pollutants In HAP/TAPS y EF Control
Alphabetical Order)
(see instructions) (Pounds/Year)
ons) Method Code (Net after all Factor
See Instructions controls)
-- 2013
Acetaldehyde 75-07-0 69.03 08 0
Formaldehyde 50-00-0 47.58 08 0
Methanol 67-56-1 301.47 08 0
30

Boise Cascade- Moncure Plywood
Emission Source: Sander System
Source ID Number: ES-04, CD-05
Emission Point: EP-05
2013 Actual Process Throughput:
Sander Operation Production 39,000,000 sf/yr
Emissions Summary: /
Compound Emission Factor Reference Emissions
M 1.15E-051b/sf 1 0.22 tpy
M-10 1.15E-05 lb/sf 1 0.22 tpy
M-2.5 1.15E-051b/sf 1 0.22 tpy
VOC 1.51E-04 lb/sf 2,3 2.95 tpy
Acetaldehyde 1.77E-06 lb/sf 2 69.03 lb/yr
Formaldehyde 1.22E-06 lb/sf 2 47.58 lb/yr
Methanol 7.73E-06lb/sf 2 301.47 lb/yr
References:
1. Stack Testing Data, 1995
2. Emission factors for VOC and organics based on NCASI Database for Wood Products
Manufactures,Updated February 2013, Sander,softwood plywood,uncontrolled median factor
3. VOC calculated as sum of VOC as C,formaldehyde,and 50%of methanol factors.

As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit : 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2013
1. Emission Source ID(from permit)or IES—GWS
Emission Source Group ID
2. Emission Source Description: Green wood fuel storage silo
3. Operating Scenario ID/Description: OS— 16/Green wood fuel storage silo
4. SCC Number/Description: 30700799/Plywood Operations ; Other Not Classified
5. Throughputlunits in 2013: 21025 TON/yr
(e.g.production or fuel use):
6. Fuel Information (1f fuel is used) %Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
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 ent lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERIDescription
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x
in 0.1 feet)
e l l.1 DOWNWARD—FACING VENT 70 1.25 72 0.45 33.13 silo vent
ep 11.2 DOWNWARD—FACING VENT 70 1.25 72 0.45 33.13 silo vent
e 11.3 DOWNWARD—FACING VENT 70 1.25 72 0.45 33.13 silo vent
ep 11.4 DOWNWARD—FACING VENT 70 1.25 72 0.45 33.13 silo vent
63

Operating Scenario: OS— 16 Emission Source/Group ID: IES—GWS
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
' 11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% arch—May 25% une—Aug. 25% Sept.—Nov. 25%
013 013 �013 013
13. Actual Emissions per Pollutant Listed
f Attach calculations and documentation of emission factors or other estimation methods used.
r.
_ Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Y See Instructions all controls
2013
' i
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po�QS Code Pollutants Method Code (Net after Factor Ef Control
Pollutantss
f (Tons/Year) (See Instructions) all controls)
2013
CO CO 08
NOx NOx 08
TSP TSP 0.01 08 0.00105
PM10 PM10 0.01 08 0.000498
j PM2.5 PM2.5 0 08 0.0000754
S02 S02 08
VOC VOC 08
Emission
HAP/TAP Emissions Control
Pollutants (In CAS HAP/TAPS Estimation Efficiency Factor Emission
(see instructions) Method Code EF Control
h Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2013
,t
1 -F
I
64

0
Boise Cascade - Moncure Plywood W
Emission Source: Hog Fuel Storage Silo
Source ID Number: IES-GWS (ES-11)
Emission Point: EP-11
2013 Actual Process Throughput:
Hog Fuel 21,025 ton/yr
Emissions Summary:
Emissions are calculated use the"drop loading equation" from AP-42 Section
13.2.4(Aggregate Handling and Storage Piles),November 2006.
AP-42 Section 13.2.4: (u)1.3
E(lh/ton) =k x 0.0032 x 5
where: (m)1-4 2
E= emission factor
k= particle size multiplier(dimensionless)
U= mean wind speed(mph)
M= material moisture content(%)
k= 0.74 For PM
k= 0.35 For PMIO
k= 0.053 For PM2.5
U= 6.88 mph for Charlotte,NC (nearest major city)from 2008-2012 Charlotte met data
M= 4.8 %based on facility estimate
Therefore,emission factors(lb PM per ton)_
PM factor= 1.05E-03 lb/ton
PMI0 factor= 4.98E-04 lb/ton
PM2.5 factor= 7.54E-05 lb/ton
Compound Emission Factor I Emissions
PM 1.05E-03 lb/ton 1 0.011 Itpy
PM10 4.98E-04 lb/ton I 0.005 tpy
PM2.5 7.54E-05 lb/ton 1 0.00 11 tpy

As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit : 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2013
1. Emission Source ID(from permit)or ES 12
Emission Source Group ID
2. Emission Source Description: dry wood residual storage silo that receives material from the dry wood residual
system cyclone ES03
3. Operating Scenario ID/Description: OS — 17/dry wood residual storage silo
4. SCC Number/Description: 30700799/Plywood Operations ; Other Not Classified
5. Throughputtunits in 2013: 128713000 FT2/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information :
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-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 IVERTICAL STACKI 60 0.7 72 0.45 13.57 silo e
31

I
I

1 !
Operating Scenario: OS— 17 Emission Source/Group ID: ES12
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
, i
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% arch—May 25% une—Aug. 25% �013
ept.—Nov. 25%
013 013 �013
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
' 2013
_ w
i Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAAQS) Code Pollutants Method Code (Net after Factor Ef Control
-t Pollutants
(Tons/Year) (See Instructions) all controls)
2013
CO CO 08 0
NOx NOx 08 0
TSP TSP 0.6 10 99.9
-- . PM10 PM10 0.6 10 99.9
PM2.5 PM2.5 0.6 10 99.9
S02 S02 08 0
4
VOC VOC 08 0
HAP/TAP CAS Emissions Emission Control
Pollutants (In HAP/TAPS Estimation Emission
I
(see instructions) Method Code Efficiency Factor EF Control
" Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2013
4
32

0
Boise Cascade-Moncure Plywood
Emission Source: Dry Waste System-Dry Waste Storage Silo
Source ID Number: ES-12, CD-21
Emission Point: EP-06,EP-12
i �
2013 Actual Process Throughput:
Plywood Production 128,713,000 sf/yr
Emissions Summary:
'- Compound Emission Factor Reference Emissions
PM 9.29E-061b/sf 1 0.60 tpy
M-10 9.29E-061b/sf 1 0.60 tpy
M-2.5 9.29E-06 lb/sf 1 0.60 tpy
References
1. Emission factor from original Title V Permit Application
I. I
r
4
i P

i
_, _ r � � � 1
� i
� � „-�

As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit : 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2013
1. Emission Source ID(from permit)or ES 13—GMO
Emission Source Group ID
2. Emission Source Description: glue mixing,application and hot press operations, including curtain coater,
plywood spreader,25 press and 40 press and paper overlay operation
3. Operating Scenario ID/Description: OS — 10/glue mixing,application and hot presses operations(Hardwood)
4. SCC Number/Description: 30700780/Plywood Operations ; Plywood Press: Phenol—formaldehyde Resin
5. Throughput/units in 2013: 83635000 FT2/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) % Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
er;-13FUGITIVE (NO 3.05 125 Area erp for gluing and
STACK) = press operations
33

rs_
i
Operating Scenario: OS— 10 Emission Source/Group ID: ES13—GMO
1-,
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
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 25/0 25/0
�013 013 �013 013
r— 13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions) all controls
� 2013
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAAQS) Code Pollutants Method Code Ef Control
Pollutants (Net after Factor
(Tons/Year) (See Instructions) all controls)
2013
CO CO 08
NOx NOx 08
TSP TSP 8.36 08 0.0002
PM10 PM10 8.36 08 0.0002
PM2.5 PM2.5 3.48 08 0.0000832
S02 S02 08
VOC VOC 4.27 08 0.000102
Emission Control
- HAP/TAP CAS Emissions Estimation Efficiency Emission
Pollutants (In see instructions HAP/TAPS EF Control
( ) Method Code (Net after all Factor
Alphabetical Order) (Pounds/Year)
See Instructions controls)
2013
Formaldehyde 50-00-0 256.75945 08 0.00000307
Methanol 67-56-1 1831.6065 08 0.0000219
Phenol 108-95-2 1329.7965 08 0.0000159
I
34

As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit : 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2013
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. Throughputtunits in 2013: 45078000 FT2/yr
(e.g.production or fuel use):
6. Fuel Information (if fuel is used) %Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
I i
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
Fe;—13FUGITIVE(NO 3 erp for gluing and
13 STACK .05 125 Area= press operations
35

i
Operating Scenario: OS—28 Emission Source/Group ID: ES 13—GMO
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% 25% 1013
une—Aug. 25% �013
ept.—Nov. 25%
013 �arch—May
13
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons ear) See Instructions all controls
f 2013
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po� Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
t,
(Tons/Year) (See Instructions) all controls)
2013
CO CO 08
NOx NOx 08
TSP TSP 4.51 08 0.0002
PM10 PM10 4.51 08 0.0002
PM2.5 PM2.5 1.88 08 0.0000832
S02 S02 08
VOC VOC 7.53 08 0.000334
Emission Control
HAP/TAP CAS Emissions Estimation Efficiency Emission
Pollutants (In HAP/TAPS y EF Control
Alphabetical Order)
(see instructions) (Pounds/Year) Method Code (Net after all Factor
See Instructions controls)
2013
Acetaldehyde 75-07-0 162.73158 08 0.00000361
I, Formaldehyde 50-00-0 100.52394 08 0.00000223
Methanol 67-56-1 2727.219 08 0.0000605
Methyl ethyl ketone 78-93-3 36.60334 08 8.12E-7
Methyl isobutyl 108-10-1 36.82873 08 8.17E-7
ketone
Phenol 108-95-2 122.16138 08 0.00000271
i
36

Boise Cascade- Moncure Plywood
Emission Source(s): Glue Operations and Pressing
Source ID Number(s): ES-13
Emission Point: EP-13
2013 Actual Process Throughput: I
Total Hardwood Production 83,635,000 sf/yr D ��
Total Softwood Production 45,078,000 sf/yr C�� (]S
Hardwood Softwood Total
Compound Emission Units Ref. Units Ref.Emissions Emission Emissions Emissions
Factor . ton/ r Factor ton/ r ton/ r
PM 2.00E-04 lb/sf 1 8.36 v 2.00E-04 lb/sf 1 4.51 ✓ 12.87
PM10 2.00E-04 lb/sf 1 8.36 ./ 2.00E-04 lb/sf l 4.51 ✓ 12.87
PM2.5 8.32E-05 lb/sf 1 3.48 8.32E-05 lb/sf 1 1.88 5.35
VOC 1.02E-04 lb/sf 1 4.27 V I 3.34E-04 Ib/sf I 1 1 7.52 ✓ 11.80
Emission Emissions Emission Emissions Total
Compound Factor Units Ref. Factor Units Ref. Emissions
Ib/ r lb/ r Ib/ r
Acetaldehyde -- 1 3.61 E-06 lb/sf 1 162.73 162.73
Formaldehyde 3.07E-06 lb/sf 1 256.76 2.23E-06 lb/sf 1 100.52✓ 357.28
Methanol 2.19E-05 Ib/sf 1 1831.61 " 6.05E-05 lb/sf 1 2,727.22 4,558.83
Methyl Ethyl Ketone -- 1 8.12E-07 lb/sf 1 36.60 36.60
Methyl Isobutyl Ketone -- 1 8.17E-07 lb/sf 1 36.83 36.83
Phenol 1.59E-05 lb/sf 1 1329.80 ` 2.71E-06 ]b/sf 1 122.16 . 1,451.96
References:
1. NCASI Wood Products Database,Updated February 2013,median value, "--"signifies non-detect. Mill uses PF resin,so PF
factors are used when available.Hardwood HAPs are not available for PF resin,so OF resin is used as best available data.
VOC factor is VOC as Carbon,converted to propane,adding formaldehyde and half of methanol.
PM 10 is assumed to equal PM,and PM2.5 is assumed to equal condensable PM. Softwood factors for PM are used,as
hardwood factors are not available.

As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit: 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2013
1. Emission Source ID(from permit)or Group G-27 consisting of ES14,ES17
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 2013: 35823 TON/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /a Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information :
Order CS—ID CD ID Control Device Description
as listed inpermit)
I CS-12 CD 18 Cyclone 60 inches in diameter
2 CS-12 CD03—WWTC Woodwaste transfer cyclone 154 inches in diameter
3 CS-12 CD06 Ba filter(7,095 square feet of filter area
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter 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 RO » 31749.72 transfer cyclone and
bagfilter
25

r—.
i
Operating Scenario: OS —20 Emission Source/Group ID: G-27
t
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% arch—May 25% une—Aug. 25% Sept.—Nov. 25%
013 013 �013 013
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
(Tons/Ye az See Instructions all controls
2013
Criteria Emissions— Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission Ef Control
Code Method Code et after Factor
Pollutants (N
Pollutants (Tons/Year) (See Instructions) all controls)
2013
CO CO 08 0
NOx NOx 08 0
TSP TSP 0.47 02 99.7 AFTER
PM10 PM10 0.47 02 99.7 AFTER
PM2.5 PM2.5 0.47 02 99.7 AFTER
S02 S02 08 0
VOC VOC 08 0
HAP/TAP CAS Emissions Emission Estimation Control Emission
Pollutants (In (see instructions) HAP/TAPS Efficiency Factor EF Control
Method Code
Alphabetical Order) (Pounds/Year) (Net after all controls)
j See Instructions
-" 2013
26

r—�
l '
Boise Cascade- Moncure Plywood
Emission Source: Green Chip Sizing,Rechip,Transfer
Source ID Number: ES-17,ES-18,ES-14 „ r>
Emission Point: EP-14
2013 Actual Process Throughput:
Tons Green Chips 35,823 ton/year
Emissions Summary:
l Compound Emission Factor Reference Emissions
M 5.30E-02 lb/DT 1 0.47 tpy
M-10 5.30E-02 lb/DT 1 0.47 tpy
M-2.5 5.30E-02 lb/DT 1 0.47 tpy
References:
1. Weyerhaeuser Test Data,Title V Bulletin#19
i_.

As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit : 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2013
1. Emission Source ID(from permit)or ES 16
Emission Source Group ID
2. Emission Source Description: Plywood waste hog
3. Operating Scenario ID/Description: OS—9/plywood hog
4. SCC Number/Description: 30700710/Plywood Operations ; Sawing
5. Throughput/units in 2013: 13440 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 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 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
39

Operating Scenario: OS —9 Emission Source/Group ID: ES16
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
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:
j an—Feb +Dec 25% 25% une—Aug. 25% Sept.—Nov. 25%
013 �arch—May
13 �013 013
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2013
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAAQS) Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2013
CO CO 08 0
NOx NOx 08 0
TSP TSP 0.36 02 99.9 0.053 AFTER
- PM10 PM10 0.36 02 99.9 0.053 AFTER
PM2.5 PM2.5 0.36 02 0 0.053 AFTER
S02 S02 08 0
VOC VOC 08 0
Emission
HAP/TAP Emissions Control
Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) See Instructions) (Net after all controls)
2013
40

r '
Boise Cascade-Moncure Plywood
Emission Source: Plywood Waste Hog
Source ID Number: ES-16Ij b5
Emission Point: EP-16
2013 Actual Process Throughput:
Tons Dry Wood 13,440 ton/year
Emissions Summary:
ri
Compound Emission Factor Reference Emissions
PM 5.30E-02 lb/DT 1 0.36 tpy
PM-10 5.30E-02 lb/DT 1 0.36 tpy
PM-2.5 5.30E-02 lb/DT 1 0.36 tpy
References:
1. Weyerhaeuser Test Data,Title V Bulletin#19
I ,
f
' I

As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit : 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2013
1. Emission Source ID(from permit)or IES 19
Emission Source Group ID
2. Emission Source Description: Diesel—fired water pump(250 Horsepower maximum power output)for
emergency purposes only
3. Operating Scenario ID/Description: OS— 11/250 horsepower diesel—fired water pump
4. SCC Number/Description: 20200407/Diesel ; Exhaust
5. Throughputtunits in 2013: 57.9 E6BTU/yr
(e.g.production or fuel use):
6. Fuel Information (1f fuel is used) %Sulfur 0.002 /o Ash Heat Content 133332 Btu/gallon
Btu/units)
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
Ferp—wp VERTICAL STACK 8 0.42 72 1 8.31 erp for diesel—fired
water pump
65

r
Operating Scenario: OS- 11 Emission Source/Group ID: IES19
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
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 ut:
an-Feb +Dec une-Au S013 et Nov.
013
25%o �arch-May
13 25% i013 g' 25% p 25%
- 13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
F- Emissions- Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
j ( 2013
Criteria Emissions- Emission Control
- Pollutant Criteria Estimation Efficient Emission Ef Control
Pollutants y
Po� Code Pollutants Method Code (Net after Factor
v�
(Tons/Year) (See Instructions) all controls)
2013
CO CO 0.03 08 0.95
NOx NOx 0.13 08 4.41
TSP TSP 0.01 08 0.31
PM10 PM10 0.01 08 0.31
PM2.5 PM2.5 0.01 08 0.31
S02 S02 0.01 08 0.29
VOC VOC 0.01 08 0.35
Emissions Emission Control
HAP/TAP CAS Estimation Efficiency Emission
r= Pollutants (In Alphabetical Order) (see instructions HAP/TAPS ll EF Control
) (Pounds/Year) Method Code (Net after all Factor
See Instructions controls)
2013
Acetaldehyde 75-07-0 0.04441 08 0.000767
i Acrolein 107-02-8 0.00536 08 0.0000925
Benzene 71-43-2 0.05402 08 0.000933
Formaldehyde 50-00-0 0.06832 08 0.00118
` Naphthalene(Component of
4 POMT 91-20-3 0.00491 08 0.0000848
Polycyclic Organic Matter
(Inc PAH,dioxins,etc.NC POM 0.00973 08 0.000168
AP 42 historic amorphous
lob
j X lene 1330-20-7 0.0165 08 0.000285
66

r�
i
Boise Cascade-Moncure Plywood
Emission Source: 250 HP Diesel-Fired Water Pump #1
f Source ID Number: ES-19
2013 Actual,Process Throughput:
a �
_h Hours of Operation 91 Hr/yr
No.2 Fuel Oil Usage 413 gal/yr
Heat Input(250 hp) 57.9 MMBtu/yr
Compound Emission Factor Units Reference Emissions
ton/
CO .9.50E-01 lb/M vMtu 1 0.027
Ox 4.41E+00 lb/MNBtu 1 0.1276✓
J PM 3.10E-01 lb/NIlVIBtu 1 0.009 ✓
PM10 3.10E-01 lb/MNBtu 1 0.009
PM2.5. 3.10E-01 lb/MNMtu 1 0.009
S02 2.90E-01 lb/NE\4Btu 1 8.39E-03
VOC 3.50E-01 lb/NfMBtu 1 1.01E-02
,I Compound Emission Factor Units Reference
Emissions
lb/ r
cetaldehyde(TH) 7.67E-04 ` lb/MNMtu 1 0.044 v
Acrolein(TH) 9.25E-05 lb/MNBtu 1 0.005 ✓
- Benzene(TH) 9.33E-04 lb/MNBtu 1 0.054 ✓
Benzo(a) yrene (T) 1.88E-07 lb/NIlABtu 1 0.00001
Formaldehyde(T 1.18E-03 lb/MNBtu 1 0.068
i aphthalene (H) 8.48E-05 lb/MNBtu 1 0.005
Toluene(T 4.09E-04 lb/NBMtu 1 0.024
- ylene(TH 2.85E-04 lb/MNMtu 1 0.016
POM. 1.68E-04 lb/MNBtu 1 0.010
References:
j 1 -AP-42, Section 3.3,Table 3.3-1,October 1996
i
i

As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit : 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2013
1. Emission Source ID(from permit)or IES19
Emission Source Group ID
2. Emission Source Description: Diesel—fired water pump(250 Horsepower maximum power output)for
emergency purposes only
3. Operating Scenario ID/Description: OS —35/250 HP Diesel Fired Water Pump#2—IES23
4. SCC Number/Description: Not required by facility,will be completed by DAQ
5. Throughputtunits in 2013: 24.2 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
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
�__l i i i
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)
F
rp—wp VERTICAL STACK 8 0.42 72 1 8.31 erp for diesel—fired
water pum
68

Operating Scenario: OS -35 Emission Source/Group ID: IES 19
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
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 ut:
an-Feb +Dec 25% arch-May 25% une-Aug. 25% Sept.-Nov. 25%
013 013 �013 013
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions- Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2013
Criteria Emissions- Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po� Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
'Y (Tons/Year) (See Instructions) all controls)
2013
CO CO 0.01 08 0.95
NOx NOx 0.05 08 4.41
` TSP TSP 0 08 0.3
PM10 PM10 0 08 0.3
PM2.5 PM2.5 0 08 0.3
S02 S02 0 08 0.29
VOC VOC 0 08 0.35
-! Emissions Emission Control
HAP/TAP CAS Estimation Efficiency Emission
Pollutants (In Alphabetical Order) (see instructions HAP/TAPS ll EF Control
i ) (Pounds/Year) Method Code (Net after all Factor
See Instructions controls)
2013
Acetaldehyde 75-07-0 0.01856 08 0.000767
Acrolein 107-02-8 0.00224 08 0.0000925
Benzene 71-43-2 0.02258 08 0.000933
1 Formaldehyde 50-00-0 0.02856 08 0.00118
h Naphthalene(Component of 91-20-3 0.00205 08 0.0000848
POMT
Polycyclic Organic Matter
(Inc PAH,dioxins,etc.NC POM 0.00407 08 0.000168
AP 42 historic amorphous
lob
X lene 1330-20-7 0.0069 08 0.000285
69

i
Boise Cascade - Moncure Plywood
Emission Source: 250 HP Diesel-Fired Water Pump #2
Source ID Number: ES-23
2013 Actual Process Throughput:
Hours of Operation 38 Hr/yr
No.2 Fuel Oil Usage 295 gal/yr
Heat Input(250 hp) 24.2 MMBtu/yr
Compound Emission Factor Units Reference Emissions
ton/ r
CO 9.50E-01 lb/MMBtu 1 0.011
Ox 4.41E+00 lb/MMBtu 1 0.0533
PM 3.10E-01 lb/MMBtu 1 0.004
PM10 3.10E-01 lb/MMBtu 1 0.004
M2.5 3.10E-01 lb/MMBtu 1 0.004
S02 2.90E-01 lb/MMBtu 1 3.50E-03
VOC 3.50E-01 lb/MMBtu 1 4.23E-03
Compound Emission Factor Units Reference Emissions
Ib/ r
Acetaldehyde(TH) 7.67E-04 lb/MMBtu 1 0.019
crolein(TH) 9.25E-05 lb/MMBtu 1 0.002
Benzene(TH) 9.33E-04 lb/MMBtu 1 0.023
Benzo(a) ene (T) 1.88E-07 lb/MMBtu 1 0.000005
Formaldehyde(TH) 1.18E-03 lb/MMBtu 1 0.029
Naphthalene (H) 8.48E-05 lb/MMBtu 1 0.002
Toluene(TH) 4.09E-04 lb/MMBtu 1 0.010
Xylene(TH) 2.85E-04 lb/MMBtu 1 0.007
POM 1.68E-04 lb/MMBtu 1 0.004 .
References:
1 -AP-42, Section 3.3,Table 3.3-1,October 1996

As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit : 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2013
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 2013: 128713000 FT2/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) % Sulfur I ro Ash I I Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
ERP-20 FUGITIVE(NO 1 100 Area= 1 Vats
STACK
41

r—
I '
Operating Scenario: OS— 18 Emission Source/Group ID: ES20
( 10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
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:
a an—Feb +Dec 25% arch—May 25% une—Aug. 25% �013
ept.—Nov. 25%
013 013 �013
- 13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2013
Criteria Emissions— Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission Ef Control
Pollutants Code Pollutants Method Code (Net after Factor
(Tons/Year) (See Instructions) all controls)
2013
- CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 2.24 08
Emission Control
HAP/TAP CAS Emissions Estimation Efficiency Emission
Pollutants (In (see instructions) HAP/TAPS Method Code (Net after all Factor EF Control
Alphabetical Order) (Pounds/Year)
See Instructions controls)
2013
F-1 Acetaldehyde 75-07-0 601.08971 08 0.00000467
Methanol 67-56-1 944.75342 08 0.00000734
42

Boise Cascade-Moncure Plywood
Emission Source(s): Vat Operations 6
Source ID Number(s): ES-20
Emission Point: EP-20
2013 Actual Process Throughput:
Total Hardwood Production 83,635,000 sf/yr
Total Softwood Production 45,078,000 sFyr
Compound Emission Factor Units Reference Emissions
p ton/yr
VOC-Hardwood 1.20E-05 lb/sf 1 0.50
VOC-Softwood 7.70E-05 lb/sf 1 1.74
Total VOC 2.24 V
Compound Emission Factor Units Reference Emissions
lb/yr
Acetaldehyde 4.67E-06 lb/sf 1 601.09
Methanol 7.34E-06 lb/sf 1 944.75
References:
1. NCASI Database for Wood Products Manufactuers,update February 2013,median, Softwood
plywood log vat. VOC hardwood is sum of VOC compounds excluding pinenes;
VOC softwood is sum of VOC compounds plus pinenes. (These values are same as
AP-42 10.5,but with more significant figures.)

As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit : 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2013
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 2013: 2970 GAL/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
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)
EP-21 VERTICAL STACK 20 1 70 10 471.23 End Sealer Spray
Booth
43

j_
Operating Scenario: OS—33 Emission Source/Group ID: ES21
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
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 o une—Aug. o �013
ept.—Nov. o
` - 013 25/0 �arch—May
13 25/0 �013 25/0 25/0
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Y See Instructions all controls
r 2013
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
��QS) Ef Control
Code Pollutants Method Code (Net after Factor
Pollutants (Tons/Year) (See Instructions) all controls)
2013
CO CO 08
NOx NOx 08
TSP TSP 0.08 03
PM10 PM10 0.08 03
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 0.05 03
Emissions Emission Control
HAP/TAP CAS Estimation Emission
Pollutants (In (see instructions) HAP/TAPS Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2013
44

05
Boise Cascade-Moncure Plywood
Emission Source(s): End Sealer Spray Booth
Source ID Number(s): ES-21
Emission Point: EP-21
i
2013 Actual Process Throughput:
End Seal Material Usage 2,970 gal/yr
Estimated Overspray 30.0%
Spray Booth Filter Efficiency 97.5%
Compound Emission Factor Units Ref Emissions
ton/yr
PM 906/0 %wt 1 0.08
M10 90% %wt 1 0.08
VOC 0.4% %wt 2 0.05
Compound Emission Factor Units Ref Emissions
lb/yr
Vinyl acetate 0.031% %wt 2,3 7.37
References:
1. Conservatively assume 90%solids in material.Assume 30%overspray into filter.
2. Compound speciation from MSDS,April 2010. Specific gravity is 0.96.
3. Compound speciation from WVCO letter,April 26,2012.
r
I�

As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit : 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2013
1. Emission Source ID(from permit)or ES22
Emission Source Group ID
2. Emission Source Description: Tongue and groove saw(plywood finishing)
3. Operating Scenario ID/Description: OS—34/Tongue and Groove Saw
4. SCC Number/Description: 30700710/Plywood Operations ; Sawing
5. Throughputtunits in 2013: 220000 FT2/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-7 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)
Ferp-06 VERTICAL STACK 30 2.8 72 50 18472.56 system erp for ste
45

r-}
Operating Scenario: OS—34 Emission Source/Group ID: ES22
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
Hours per Day ( 1 ) Days per Week ( 1 ) Weeks per Year ( 30 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% arch—May 25% une—Aug. 25% Sept.—Nov. 25%
013 013 �013 013
_ 13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
+- Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2013
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po� Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
�
(Tons/Year) (See Instructions) all controls)
2013
CO CO 08 0
NOx NOx 08 0
TSP TSP 0.01 02 99.5
PM10 PM10 0 02 99.5
PM2.5 PM2.5 0 08 0
S02 S02 08 0
- VOC VOC 0.01 08 0
HAP/TAP Emissions Emission Control
CAS Estimation Efficient Emission
Pollutants (In (see instructions) HAP/TAPS Method Code (Net after all Factor EF Control
j Alphabetical Order) (Pounds/Year) See Instructions controls)
2013
Acetaldehyde 75-07-0 0.12298 08 0 5.59E-7 AFTER
Formaldehyde 50-00-0 0.08558 08 0 3.89E-7 AFTER
Methanol 67-56-1 1.5004 08 0 0.00000682 AFTER
4 JI
`Jr
46

Boise Cascade- Moncure Plywood
Emission Source: Tongue and Groove Saw
Source ID Number: ES-22, CD-06
Emission Point: EP-06
2013 Actual Process Throughput:
Saw Operating Hours 120 hours
Saw Production 220,000 sFyr
Calculations for this source is based on the following assumptions:
The T&G saw removes 0.5"per panel.
The T&G saw trims the finished plywood panels of 96"x 48". The nominal thickness is 3/8" (0.375).
The density of dry pine is 35.6 lb/ft3.
Conservatively assume baghouse efficiency of 99.5%.
Volume of Annual T&G- T&G
Compound Total Panels T&G/Panel Dust Generated Rate
(per year) (ft3/ anel) (ton/yr) (ton/hr)
P?\1 6,875 0.0104 1.275 0.011
Potential Emissions Summary
Baghouse Annual
Compound Efficiency Emissions
(%) (lb/ r) (ton/ r)
PM 99.5 12.75 0.006
PM10 z 99.5 4.09 0.002
PM2.5 z 99.5 1.82 0.001
Compound Emission Factor Reference Emissions
VOC 7.55E-05lb/sf 3 0.01 tpy
Acetaldehyde 5.59E-07 lb/sf 3 0.12 1b/yr
Formaldehyde 3.89E-07lb/sf 3 0.09lb/yr ✓
Methanol 6.82E-061b/sf 3 1.50 Ib/yr .i
References:
1. Emission rates for PM based on estimated amount of trim and dust generated and conservative
baghouse efficiency of 99.5%.
2. AP-42 Appendix 13.1, Section 10.5,October 1986. PM10 is assumed to be 32.1%of PM from
sander cyclone and baghouse. PM2.5 is assumed to be 14.3%of PM from sander cyclone and baghouse.
3. Emission factors for VOC and organics based on NCASI Database for Wood Products Manufactures,
updated February 2013,Sander,softwood plywood,uncontrolled median factor. VOC calculated as
sum of VOC as C,formaldehyde,and 50%of methanol factors.

As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit : 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2013
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 2013: 21025 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
47

Operating Scenario: OS—2 Emission Source/Group ID: I-1
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
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 o une—Aug. o �013
ept.—Nov. o
2013 25/0 �arch—May
13 25/0 �013 25/0 25/o
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2013
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAAQS) Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2013
CO CO 08
NOx NOx 08
TSP TSP 0.01 08
PM10 PM10 0.01 08
PM2.5 PM2.5 0 08
S02 S02 08
VOC VOC 08
HAP/TAP Emissions Emission Control
Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission
(see instructions) EF Control
Alphabetical Order) (Pounds/Year) Method Code Factor
See Instructions) (Net after all controls)
2013
48

Boise Cascade-Moncure Plywood 1,
Emission Source: Bark Hog
Source ID Number: IS-IN-1
Emission Point: IS-IN-1
2013 Actual Process Throughput:
Fuel Hogged 21,025 ton/yr
Emissions Summary:
Emissions are fugitive in nature.
Specific emission factors are not available for hogging operations. Hogging emissions are assumed to be
similar to emissions from debarking. PM emissions for debarking are based on the former AP-42 emission
factor for drum debarkers and total amount of green material processed by the hogs;PM2.5 = 19%of PM.
The hog is located inside a building. A 95%control has been applied to account for building control.
PM 0.024 lb/ton
PM10 0.011 lb/ton
PM2.5 0.0046 lb/ton
Green Emission Inside Annual Annual
Compound Material Factor Building Emissions Emissions
(t y) (lb/ton) Control(%) (lb/yr) (TPY)
PM 21,025 0.024 95% 25.23 0.01
PM10 1 21,025 1 0.011 1 95% 11.56 0.01
PM2.5 1 21,025 1 0.0046 1 95% 4.79 0.002

As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit : 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory-Calendar Year 2013
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 2013: 717 TON/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) % Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS-ID CD ID Control Device Description
as listed inpermit)
17--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)
F
P-FUG FUGITIVE(NO 1 72 Area= 1 ERP for Fugitive
STACK) sources
53

Operating Scenario: OS —3 Emission Source/Group ID: I-2
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% arch—May 25% une—Aug. 25% Sept.—Nov. 25%
- 013 013 �013 013
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
(Tons/Year) See Instructions all controls
2013
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAAQS) Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
- 2013
CO CO 08
NOx NOx 08
TSP TSP 0 08
PM10 PM10 0 08
PM2.5 PM2.5 0 08
S02 S02 08
VOC VOC 08
_ HAP Emission/TAP CAS Emissions Estimation Control Emission
Pollutants (In (see instructions) HAP/TAPS Efficiency Factor EF Control
Method Code
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2013
i '
54

Boise Cascade- Moncure Plywood
Emission Source: Core Chipping
Source ID Number: IS-IN-2
Emission Point: IS-IN-2
2013 Actual Process Throughput:
Cores Chipped 717 ton/year
Emissions Summary:
Emissions are fugitive in nature.
Specific emission factors are not available for chipping operations. Chipping emissions are assumed to be
similar to emissions from debarking. PM emissions for debarking are based on the former AP-42 emission
factor for drum debarkers and total amount of green material processed by the chipper;PM2.5= 19%of PM.
The chipper is located inside a building. A 95%control has been applied to account for building control.
PM 0.024 lb/ton
PM 10 0.011 lb/ton
PM2.5 0.0046 lb/ton
Green Emission Inside Annual Annual
Compound Material Factor Building Emissions Emissions
(tpy) (lb/ton) Control(%) (lb/yr) (TPY)
PM 717 0.024 95% 0.86 0.0004
PM10 717 0.011 95% 0.39 0.0002
PM2.5 717 1 0.0046 1 95% 1 0.16 1 0.0001

As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit : 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory-Calendar Year 2013
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 2013: 35106 TON/yr
(e.g.production or fuel use):
6. Fuel Information (1f 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
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)
7EP-FUG FUGITIVE(NO 1 72 Area= 1 ERP for Fugitive
STACK) sources
55

r
Operating Scenario: OS—4 Emission Source/Group ID: I-3
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
— 12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% arch—May 25% �une—Aug. 25% Sept.—Nov. 25%
013 013 013 013
-- 13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
_. Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
(Tons/Ye az See Instructions all controls
2013
Criteria Emissions— Emission Control
,/N ^■.0 Pollutant Criteria Estimation Efficiency Emission
Pollutants
Code Pollutants Method Code (Net after Factor Ef Control
Pollutants (Tons/Year) (See Instructions) all controls)
- 2013
CO CO 08
NOx NOx 08
- TSP TSP 0.02 08
PM10 PM10 0.01 08
PM2.5 PM2.5 0 08
S02 S02 08
VOC VOC 08
HAP/TAP Emissions Emission Control
Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code Factor
� Alphabetical Order) (Pounds/Yeaz) (Net after all controls)
See Instructions
2013
56

Boise Cascade - Moncure Plywood
Emission Source: Green Veneer Hogging Operations
Source ID Number: IS IN-3
Emission Point: IS_IN-3 �Dc
2013 Actual Process Throughput:
Green Veneer Hogged 35,106 ton/year
Emissions Summary:
Emissions are fugitive in nature.
Specific emission factors are not available for hogging operations. Hogging emissions are assumed to be
similar to emissions from debarking. PM emissions for debarking are based on the former AP-42 emission
factor for drum debarkers and total amount of green material processed by the hogs;PM2.5 = 19%of PM.
The hog is located inside a building. A 95%control has been applied to account for building control.
PM 0.024 lb/ton
PM 10 0.011 lb/ton
PM2.5 0.0046 lb/ton
Green Emission Inside Annual Annual
Compound Material Factor Building Emissions Emissions
(t y) (lb/ton) Control(%) (lb/yr) (TPY)
PM 35,106 0.024 95% 42.13 0.02
13M10 1 35,106 1 0.011 1 95% 19.31 1 0.01
PM2.5 1 35,106 1 0.0046 1 95% 8.00 1 0.004

As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit : 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2013
1. Emission Source ID(from permit)or Group G-25 consisting of I-4,1-5
Emission Source Group ID
2. Emission Source Description: Ink and painting operations
3. Operating Scenario ID/Description: OS—5/Ink and painting operations
4. SCC Number/Description: 40500597/Printing—General;Other Not Classified
5. Throughput/units in 2013: 1335 GAL/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
EP—FUG FUGITIVE(NO 1 72 Area= I ERP for Fugitive
STACK) sources
23

I
I
Operating Scenario: OS—5 Emission Source/Group ID: G-25
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
r`
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% 25% une—Aug. 25% �013
ept.—Nov. 25%
013 �arch—May
13 �013
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
s Emissions— Emission Control
Y GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Y See Instructions all controls
I �
2013
i Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po� Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2013
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
I PM2.5 PM2.5 08
S02 S02 08
VOC VOC 0.55 03
Emission
HAP/TAP CAS Emissions Estimation Control Emission
Pollutants (In ( ) HAP/TAPS Method Code Efficiency EF Control
see instructions Factor
i Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2013
I
_ 1
_r
,
24

" lC
i I
f�
Boise Cascade-Moncure Plywood
Emission Source: Ink and Painting Operations
Source ID Number: IS-IN-4,IS-IN-5
Emission Point: IS-IN-4,IS-IN-5
2013 Actual Process Throughput:
— Logo paint usage 880 gal/yr
Ink usage 455 gal/yr
Ink density 8.21 lb/gal
k Emissions Summary:
Compound Emission Factor Reference Emissions
If
VOC-logo.paint I 4.00E-01 jib VOC/gal I 1 1 0.18 tpy
VOC-ink I 2.00E-01 Ilb VOC/lb I 1 1 0.37 tpy
Total VOC 0.55,tPY
References:
i F 1. Material Safety Data Sheets
r
I
i-r

As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit: 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2013
1. Emission Source ID(from permit)or I-6
Emission Source Group ID
2. Emission Source Description: Plywood surface patching
3. Operating Scenario ID/Description: OS—6/Plywood surface patching
4. SCC Number/Description: 30700799/Plywood Operations ; Other Not Classified
5. Throughput/units in 2013: 37499 GAL/yr
1` (e.g.production or fuel use):
6. Fuel Information (If fuel is used) % Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8.-Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
EP—FUG FUGITIVE(NO 1 72 Area= 1 ERP for Fugitive
STACK) sources
57

i
Operating Scenario: OS —6 Emission Source/Group ID: I-6
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% arch—May 25% une—Aug. 25% �013
ept.—Nov. 25%
013 013 �013
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
_ Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2013
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAAQS) Ef Control
Code Pollutants Method Code (Net after Factor
Pollutants
(Tons/Year) (See Instructions) all controls)
2013
_ CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 0.01 03
Emission
HAP/TAP Emissions Control
Pollutants (In CAS HAP/TAPS Estimation Efficiency Factor Emission
(see instructions) Method Cod
EF Control
e
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2013
,
f
58

31 `
Boise Cascade- Moncure Plywood
Emission Source: Plywood Surface Patching
Source ID Number: IS-IN-6
Emission Point: IS-IN-6
2013 Actual Process Throughput:
Plywood Surface Patching(Part A) 8,084 gaUyr
Density 12.58 lb/gal
Plywood Surface Patching(Part B) 29,415 gaUyr
Density 10.33 lb/gal
Emissions Summary:
Compound %Wt Reference Emissions
Fraction lb/ r tons/ r
VOC 0.02% 1,2 20.34 0.01
4,4 Diphenylmethane Diisocyanate(MDI) 38% 1 negligible negligible
References:
1. Material Safety Data Sheet for U-100-B Patch Catalyst,April 2014. Due to the extremely low vapor /
pressure of the material(<0.000001 mmHg)per the manufacturer's MSDS,VOC and HAP emissions
from the use of this product are assumed to be negligible. (The MSDS shows 0%VOC.)
2. Material Safety Data Sheet for U-100-A Patch,April 2014.

As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit : 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2013
1. Emission Source ID(from permit)or I-7
Emission Source Group ID
2. Emission Source Description: Maintenance parts washers
3. Operating Scenario ID/Description: OS —7/Maintenance parts washer
4. SCC Number/Description: 40202105/Flatwood Products Coating;Equipment Cleanup
5. Throughput/units in 2013: 55 GAL/yr
(e.g.production or fuel use):
6. Fuel Information (1f 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)
�7--, 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 ft (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
EP—FUG FUGITIVE(NO 1 72 Area= 1 ERP for Fugitive
STACK) sources
59

r-r
Operating Scenario: OS—7 Emission Source/Group ID: I-7
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
, J
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% arch—May 25% une—Aug. 25% Sept.—Nov. 25%
` 013 013 013 013
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
_ Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2013
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
��QS) Ef Control
Code Pollutants Method Code (Net after Factor
Pollutants
? (Tons./Year) (See Instructions) all controls)
2013
CO CO 08
NOx NOx 08
TSP TSP 08
r. PM10 PM10 08
' PM2.5 PM2.5 08
S02 S02 08
VOC VOC 0.19 03
- HAP/TAP CAS Emissions Emission Estimation Control Emission
Pollutants (In (see instructions) HAP/TAPS Efficiency Factor EF Control
Method Code
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2013
60

r�
l� /X
Boise Cascade-Moncure Plywood
Emission Source: Maintenance Parts Washer
Source ID Number: IS-IN-7
Emission Point: IS-IN-7
2013 Actual Process Throughput:
Gallons Used 55 gal/yr
Emissions Summary:
Compound Emission Factor Reference Emissions
--, VOC I 7.00E+00 lb/gal I 1 1 0.19 tpy
r
-" References:
1. Material Safety Data Sheet
r ,
l l

As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit : 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory-Calendar Year 2013
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 2013: 173462 TON/yr
(e.g.production or fuel use):
6. Fuel Information (if fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS-ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-FUG FUGITIVE(NO 1 72 Area= 1 ERP for Fugitive
STACK) sources
61

r-
Operating Scenario: OS—8 Emission Source/Group ID: I-8
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
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 o une—Aug. o �013
ept.—Nov. o
013 25/a �arch—May
13 25/0 �013 25/0 25/0
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Y See Instructions all controls
2013
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po�QS Code Pollutants Method Code (Net after Factor Ef Control
Pollutantss
(Tons/Year) (See Instructions) all controls)
2013
CO CO 08
NOx NOx 08
TSP TSP 2.3 02
PM10 PM10 2.3 02
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP CAS Emissions Emission Estimation Control Emission
Pollutants (In HAP/TAPS Efficiency EF Control
(see instructions) Method Code
Alphabetical Order) (Pounds/Year) (Net after all controls) Factor
See Instructions
2013
62

Boise Cascade-Moncure Plywood o
Emission Source: Veneer Diverter Exhaust Cyclone
Source ID Number: IS-IN-8
h
Emission Point: IS-IN-8
2013 Actual Process Throughput:
Green Veneer 173,462 ton/yr
Emissions Summary:
Compound Emission Factor Reference Emissions
M 5.30E-02 lb/DT 1 2.30 tpy
PM-10 I 5.30E-02 lb/DT 1 1 1 2.30 t2y
References:
1. Weyerhaeuser Test Data,Title V Bulletin#19,max green chips factor
I '
r_

As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit : 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2013
1. Emission Source ID(from permit)or Group GR2 consisting of I-10, 1-9
Emission Source Group ID
2. Emission Source Description: Green Veneer Stackers
3. Operating Scenario ID/Description: OS —32/Green Veneer Stackers
4. SCC Number/Description: 30700799/Plywood Operations ; Other Not Classified
5. Throughput/units in 2013: 173462 TON/yr
(e.g.production or fuel use):
6. Fuel Information (1f fuel is used) ro
Sulfur %Asli 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 1 72 Area= 1 Stackers
g STACK
5

I
Operating Scenario: OS—32 Emission Source/Group ID: GR2
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% 25% une—Aug. 25% �013
ept.—Nov. 25%
0.13 �arch—May
13 �013
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
TonsNear See Instructions all controls
2013
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficient Emission
Po�QS Code Pollutants Method Code (Net after Factor Ef Control
Pollutantss
i (Tons/Year) (See Instructions) all controls)
-- 2013
CO CO 08
NOx NOx 08
TSP TSP 0.61 08
PM10 PM10 0.61 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP Emissions Emission Control
Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) See Instructions) (Net after all controls)
'
2013
6

Boise Cascade- Moncure Plywood
Emission Source: Green Veneer Stackers
Source ID Number: IS-IN-9, IS-IN-10
Emission Point: IS-IN-9, IS-IN-10
2013 Actual Process Throughput:
Green Veneer 173,462 tons/yr
Emissions Summary:
Compound Emission Factor Reference Stacker
Emissions
PM I 1.40E-02 lb/DT 1 1 0.61 tpy
PM-10 I 1.40E-02 lb/DT 1 1 0.61 tpy
References:
1. Weyerhaeuser Test Data,Title V Bulletin#19,average green chips factor

As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit: 03424
Moncure,NC 27559 County: Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory-Calendar Year 2013
1. Emission Source ID(from permit)or 1-11
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 2013: 4836 TON/yr
(e.g.production or fuel use):
6. Fuel Information (1f fuel is used) % 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)
�777-1 i i I
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-Fug3 FUGITIVE(NO 1 72 Area- 1 Hammer Hog Truck
STACK) Dump
49

Operating Scenario: OS—25 Emission Source/Group ID: I-11
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% 25% une—Aug. 25% �013
ept.—Nov. 25%
013 �arch—May
13 �013
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
! GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2013
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAAQS) Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2013
r -
CO CO 08
1 NOx NOx 08
TSP TSP 0 08
PM10 PM10 0 08
PM2.5 PM2.5 0 08
S02 S02 08
VOC VOC 08
I— HAP/TAP Emissions Emission Control Emission
(see instructions) Method Code Factor
Pollutants (In CAS HAP/TAPS Estimation Efficiency EF Control
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2013
� 4
I
11
i '
50

r�
Boise Cascade-Moncure Plywood %
Emission Source: Hammer Hog Truck Dump
Source ID Number: IS-IN-I1
Emission Point: IS-IN-11
2013 Actual Process Throughput:
Dry waste 4,836 ton/yr
Emissions Summary:
Emissions are calculated use the"drop loading equation" from AP-42 Section
13.2.4(Aggregate Handling and Storage Piles),November 2006.
U 13
AP-42 Section 13.2.4: 5
E (lb/ton) =k x 0.0032 x (m)1.4
where: ` 2
E= emission factor
k= particle size multiplier(dimensionless)
U= mean wind speed(mph)
M= material moisture content M)
k= 0.74 For PM
k= 0.35 For PMIO
k= 0.053 For PM2.5
U= 6.88 mph for Charlotte,NC(nearest major city)from 2008-2012 Charlotte met data
M= 4.8 %based on facility estimate
Therefore,emission factors(lb PM per ton)_
PM factor= 1.05E-03 lb/ton
PMIO factor= 4.98E-04 lb/ton
PM2.5 factor= 7.54E-05 lb/ton
Compound Emission Factor Emissions
PM 1.05E-03 lb/ton 0.003 tpy
PMIO 4.98E-04 lb/ton 0.001 t y
PM2.5 7.54E-05 lb/ton 0.00021tpy

As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit : 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2013
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 2013: 1843 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)
�77-1 i i -
9.Emission Release Point RP Information: Sources vented to more than one ERP use additional entry fines :
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
EP—Fug2 FUGITIVE(NO 1 72 Area= 1 Dry Waste Truck
STACK) Dump
51

r—
Operating Scenario: OS —24 Emission Source/Group ID: I-12
? 10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% 25% une—Aug. 25% Sept.—Nov. 25%
013 �arch—May
13 �013 013
13. Actual Emissions per Pollutant Listed :
f Attach calculations and documentation of emission factors or other estimation methods used.
� r
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Y See Instructions all controls
I 2013
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAA Code Pollutants Method Code (Net after Factor Ef Control
Pollutants (Tons/Year) (See Instructions) all controls)
2013
CO CO 08
NOx NOx 08
TSP TSP 0 08
PM10 PM10 0 08
I
PM2.5 PM2.5 0 08
S02 S02 08
VOC VOC 08
HAP/TAP Emissions Emission Control
CAS Estimation Emission
Pollutants (In (see instructions) HAP/TAPS Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) See Instructions) (Net after all controls)
2013
I
r >
52

PK
Boise Cascade- Moncure Plywood
Emission Source: Dry Waste Truck Dump
Source ID Number: IS-IN-12
Emission Point: IS-IN-12
2013 Actual Process Throughput:
Dry waste 1,843 ton/yr
Emissions Summary:
Emissions are calculated use the"drop loading equation"from AP-42 Section
13.2.4(Aggregate Handling and Storage Piles),November 2006.
(Ull3
AP-42 Section 13.2.4: I 5 J
E(lb/ton) =k x 0.0032 x \
where: ` 2
E= emission factor
k=particle size multiplier(dimensionless)
U= mean wind speed(mph)
M= material moisture content(%)
k= 0.74 For PM
k= 0.35 For PMIO
k= 0.053 For PM2.5
U= 6.88 mph for Charlotte,NC(nearest major city)from 2008-2012 Charlotte met data
M= 4.8 %based on facility estimate
Therefore,emission factors(lb PM per ton)_
PM factor= 1.05E-03 lb/ton
PMIO factor= 4.98E-04 lb/ton
PM2.5 factor= 7.54E-05 lb/ton
Compound Emission Factor Emissions
PM 1.05E-03 lb/ton 0.001 tpy
PM10 4.98E-04 lb/ton 0.0005 tpy
PM2.5 7.54E-05 lb/ton 0.0001 t y

i ,
Appendix F
Supporting Data

As entered in AERO
Facility Name: Moncure Plywood Facility ID : 1900039
306 Corinth Road Permit : 03424
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
Comments From Facility:
6/12/2014—General Comments
General Comments: Due to extremely low vapor pressure of the material (<0.000001 mmHg) in OS-6 per the
the manufacturer's MSDS,emissions are assumed to be negligible.
General Comments: Some criteria pollutant emissions for OS-2,OS-3,OS-4,OS-6,OS-16,OS-24,OS-25,OS-34
and OS-35 are below the AFRO reporting threshold but can be viewed in the calculations.

NC DAQ - EMISSIONS fNVENTORY Page 1 of 3
NorCh Carofina Department of EnvirGnrnent
Home Emissions Flow Facility Totals ES-CD List User Manual Logoff
Operating Scenario Summary AERO
Emission Sources Emission Groups Control Devices Emission Release Points Operating Scenario Summary Closeout
PAGE INSTRUCTIONS Facility Id : 1900039 Data Year:2013
< 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)
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,
(Hardwood) V
Add New Operating Scenario
G-25 Ink and painting operations
OS5 Ink and painting operations
Add New Operating Scenario
G-27 Woodwaste Transfer system
OS20 Woodwaste Transfer(Rechipper)system
Add New Operating Scenario
ES-13-25HP 25 panel hot press
Add New Operating Scenario
ES-13-40HP 40 panel hot press
Add New Operating Scenario
ES-13-CC Curtain coater (�
Add New Operating Scenario
ES-1 3-PO Paper overlay operation
Add New Operating Scenario
ES-1 3-PS Plywood spreader (�
Add New Operating Scenario
ES03-CC Core composer with saw
Add New Operating Scenario
ES03-CS Core saw(green or dry veneer)
Add New Operating Scenario
ES03-PSS Panel sawing system
Add New Operating Scenario
}.4*na•//vonv�n ,..+�nnrnrR/or./liTl�-'iv4or...,lC......1..4�....1—T(l IIC�C__WW._�. T___ �i�� ,nn� �

NC DAQ - EMISSIONS INVENTORY Page 2 of 3
ES03-SMS-1 String machine including saws
OS21 Dry Waste transfer system
Add New Operating Scenario
ES03-SMS-2 String machine including saws
Add New Operating Scenario
ES03-SS Strip saw
Add New Operating Scenario
ESO4 Wood sander
OS12 wood sander
Add New Operating Scenario
ES12 Dry wood residual storage silo +�
OS17 dry wood residual storage silo
Add New Operating Scenario
ES13-GMO Glue mixing operations consisting of two resin storage tanks and
four mixe
OS10 glue mixing, application and hot presses operations(Hardwood)
OS28 glue mixing, application and hot presses operations, (softwood)
Add New Operating Scenario
ES15 tongue and groove operations
A_ OS19 tongue and groove operations
Add New Operating Scenario
ES16 Plywood waste hog
OS9 plywood hog
Add New Operating Scenario
ES20 Vat operations
OS18 Vat Operations: Heating of Blocks
Add New Operating Scenario
ES21 End sealer spray booth
OS33 End Sealer Spray Booth
Add New Operating Scenario
ES22 Tongue and groove saw(plywood finishing) d
OS34 Tongue and Groove Saw
Add New Operating Scenario
1-1 Bark hogging operations with two saws
OS2 Bark hogging operations
Add New Operating Scenario
1-11 hammer hog truck dump
OS25 Hammer hog truck dump- no controls
Add New Operating Scenario
1-12 dry waste truck dump
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

NC DAQ - EMISSIONS INVENTORY Page 3 of 3
1-3 Green veneer hogging
OS4 Green veneer hogging operations
Add New Operating Scenario
1-6 Plywood surface patching
OS6 Plywood surface patching
Add New Operating Scenario
1-7 Maintenance parts washers
OS7 Maintenance parts washer
Add New Operating Scenario
1-8 Veneer diverter exhaust cyclone
OS8 Veneer diverter exhaust cyclone
Add New Operating Scenario
IES-GWS Green wood fuel storage silo
OS16 Green wood fuel storage silo
Add New Operating Scenario
IES19 Diesel-fired water pump(250 Horsepower maximum power output)
for emergenc
OS11 250 horsepower diesel-fired water pump
OS35 250 HP Diesel Fired Water Pump#2-IES23
Add New Operating Scenario
< Back Continue >
.0A
Feedback MCDENR Top of Page

Boise Cascade-Moncure Plywood
Annual Activity and Usage Information
2013 Air Emissions Inventory
URS Project No.31829585
Activity and Usage 2013 Annual Amount
Hardwood Plywood Production 83,635,000 ftZ 3/8")
Softwood Plywood Production 45,078,000 ftZ 3/8")
Plywood Plywood Press Hours of Operation 7,523 hours
Production Sander Production 39,000,000 ftZ 3/8"
T&G Saw Production 220,000 ftZ 3/8"
T&G Saw Hours of Operation 120 hours
Log Pine Los 98,135 tons
Throughput Gum Los 98,111 tons
Poplar Logs 16,070 tons
Boiler Hours of Operation 8,064 hours
Total Dry Wood Combustedl 13,440 ton as fired
Dry Wood Heat Content 7,776 Btu/lb
Total Dry Wood Combusted 209,019 MMBtu/yr
Green Chips Combusted 3,000 tons chips
Green Chips Heat Content 2 4,541 Btu/lb
Total Green Chips Combusted 27,246 MMBtu
Total Hog Fuel Combustedl 21,025 ton as fired
Plant wide Fuel Poplar Bark Heat Content2 5,703 Btu/lb
Combustion Gum Bark Heat Contene 4,952 Btu/lb
Pine Bark Heat Content 4,018 Btu/lb
Total Hog Fuel Combusted 196,847 MMBtu
Total Green Fuel Combusted 224,093 MMBtu
Total of all fuel combusted 433,111 MMBtu
Boiler Efficiency 86.0% %
250 HP Diesel Fired Water Pump#1 413gal/yr
91 hr/yr
250 HP Diesel Fired Water Pump#2 295gal/yr
38 hr/yr
Veneer Diverter 173,462 ton/yr
Hammer Hog Truck Dump 4,836 ton/yr
Dry Waste Truck Dump 1,843 ton/yr
Core Chipping and Handling 717 ton/yr
Green Veneer Hogging Operations 35,106 ton/yr
Maintenance Parts Washer 55
Miscellaneous End Seal Paint 2,970 al/
yr
Paint Usage(Logo painting) 880gal/yr
Ink Usage 455gal/yr
Green Veneer Stackers 173,462 ton/yr
Plywood Surface Patching Part A 8,084gal/yr
Plywood Surface Patching Part B) 29,415gal/yr
Cores Sold in 2013 841,652 cores
Ash Total Wood Ash 413 tons
Total Wood Ash sent offsite 413 tons
PF Resin Usage PF Resin Application Rate 25 Tons/MMSF
PF Resin Usage 5,225 tons
1. Bark fired is calculated based on log usage and percentage of a log that is bark(assumes 80%of
bark originally on log is combusted). Dry fuel is estimated to be 15%of total fuel usage based on
data from Chester Plywood(sister plant).
2. Heat Content is Chester Plywood fuel analysis data.
P:Vobs4\2014Vvfooaue PlywoodWEI\M-2013 AS Cda WAS]sh\Psod Info

Boise Cascade-Moncure Plywood
Permit Limit Check
2013 Air Emissions Inventory
URS Project No.31829585
Source T23 Permit Limit 2013 Actual Emissions In Compliance?
FBB PM 15.38 1b/hr 11.47 lb/hr YES
' I
FBB SO2 2.31b/MMBtu O.00lb/M1VIBtu YES
Facility-wide Methanol(Max HAP) 10 ton/yr 4.23 1 ton/yr YES
Facility-wide Total HAP 25 ton/yr 10.91 ton/yr I YES
Acrolein 2.4 lb/hr 0.09 lb/hr YES
Arsenic 1.48 lb/yr 0.70 lb/yr YES
Benzene 772.92 lb/yr 91.02 lb/yr YES
Beryllium 26.41 1b/yr 0.011 YES
Cadmium 35.2 1b/yr 1.03 1b/yr YES
Chlorine 10 1.13 lb/day 0.51 lb/day YES
ES09 Chlorine 27.02 lb/hr 0.02 lb/hr YES
Formaldehyde 3.77 lb/hr 0.12 lb/hr YES
Hydrogen Chloride 21.02 lb/hr 0.01 lb/hr YES
Manganese 83.6 lb/day 1.60 lb/day YES
Nickel(metal) 16.19 lb/day 0.01 lb/day YES
Phenol 6.74 lb/hr 0.02 lb/hr YES
Vinyl Chloride I 38,656 lb/yr 1 19.5 01 lb/yr YES
Acrolein 2.4 lb/hr 0.09 lb/hr YES
Arsenic 1.48 lb/yr 0.70 lb/yr YES
Benzene 772.92 lb/yr 91.02 lb/yr YES
Beryllium 26.41 lb/yr 0.01 lb/yr YES
Cadmium 35.2 lb/yr 1.03 lb/yr YES
Chlorine 101.13 lb/day 0.51 lb/day YES
- ES 10 Chlorine 27.02 lb/hr 0.02 lb/hr YES
Formaldehyde 3.77 lb/hr 0.12 lb/hr YES
Hydrogen Chloride 21.02 lb/hr 0.01 lb/hr YES
Manganese 83.6 lb/day 1.60 lb/day YES
Nickel(metal) 16.19 lb/day 0.01 lb/day YES
Phenol 6.74 lb/hr 0.02 lb/hr YES
Vinyl Chloride 38,656 lb/yr 19.50 lb/yr YES
ES13 Formaldehyde 2.33lb/hr 0.05lb/hr YES
Phenol 28.62 lb/hr 0.19 1 lb/hr YES