AQ_F_7300061_20211109_EI_Cmb-EI-File

2020 Emissions Inventory Review/ Data Tracking Form
Facilih1 Name: Louisiana-Pacific Corporation -Roxboro Facilitv 1D: 7300061
Facility Assigned to: Data Entry: Person County
Classification: Matthew Mahler Confidential Copy Submitted?
Title V ~ES 0
Initial Revie,
J Enter date received into ED. Date Received: I
D Assigned to appropriate individual. Date Assigned: Date Due:
D Paper copy submitted: One copy received with supporting documentation, certification fomi signed by responsible
j' official, and appears generally complete; OR
~ Electronic copy submitted: All supporting documentat ion and certification fonn (with time/date stamp) signed by
responsible official has been received.
Inventory Review
~ All forms and supporting documentation appear to be complete if paper submission (check ED OS data if electronic).
If', Contact, address, phone number changes entered into I-Beam/Faci lities if necessary.
Iii All known operating scenarios, control devices, and emission release points have been entered for each emission
source (permitted, insignificant, and unpennitted) or note that the emission source was not operated or not required to report.
~ Check if SCC codes for each OS are accurate and update if needed.
141 Evaluate "U" sources for significance and address according to policy. si Calculations / fomis appear to add up correctly. tf All compliance issues are being addressed (e.g. Toxics limits, above TV thresholds, large emissions
increase/decrease, installation without a permit).
All volatile HAPsfrAPs 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 infomiation is required (corrections due date and date received).
Check all ED QNQC 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".
Date Info Requested: Date Info Received: Total Days on Hold:
Date Review Complete:
Date Approved:
ll\51Zo2\
II Is /zoi.. I
Signature:
Date Submitted to EI Coordinator:
') I"' ,~ \ Initials:
j)~~
d~
Facility Total CY 2020 Emission Summary Recorded in ED Facility ID #: 7300061
Facility Name: Louisiana-Pacific Corporation -Roxboro Permit #(s): 07760T24
Green House Gases Pollutants (GHG) Actual Emissions
Tons/Yr %
Pollutant CAS Demini-Change
mus
Not Not NIA
Reported Reported
CO2 equivalent (sum of individual GHG pollutant emissior No GHGs
times their 1995 IPCC Global Warming Potential (GWP), Reported
converted to metric tons)
Criteria Pollutants Actual Emissions
(Tons/Year)
Pollutant CAS CY 2020 CY 2019 Demini-%
from ED from Fees mus Change
co co 116.33 101.77 0.5 14.3%
NOx NOx 141.26 135.49 0.5 4.3%
PM(TSP) TSP 68.10 66.30 0.5 2.7%
PMI0 PMI0 66.38 64.60 0.5 2.8%
PM2.5 PM2.5 66.38 64.60 0.5 2.8%
SO2 SO2 6.84 8.8 1 0.5 -22.4%
voe voe 129.90 127.85 0.5 1.6%
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPs) (Pounds/Year)
Pollutant CAS CY2020 CY 2019 Demini-o;.,
from ED from Fees mus Change
!Antimony & Compounds (total mass, inc elemental SB) 1.82 2.14 10.0 -15.0%
Antimony Unlisted Compounds -Specify Compoun, SBC-Other 1.82 2.14 10.0 -14.6%
(Component of SBC)
Arsenic & Compounds (total mass of elemental AS, arsine and 4.70 4.66 0.01 0.9%
all inorganic compounds)
Arsenic Unlisted Compounds -Specify Compound ASC-Other 4.70 4.66 0.01 0.9%
(Component of ASC)
Beryllium & comp ounds (Total mass) 0.254230 0.297710 1.0 -14.6%
Beryllium Metal (unreacted) (Component of BEC) 7440-41-7 0.254230 0.297710 1.0 -14.6%
Cadmium & compounds (total mass includes elemental metal) 1.18 1.33 0.1 -11.3%
11/05/2021 Page l of 5
Facility Total CY 2020 Emission Summary Recorded in ED Facility ID #: 7300061
Facility Name: Louisiana-Pacific Corporation -Roxboro Permit #(s): 07760T24
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPs) (Pounds/Year)
Pollutant CAS CY2020 CY 2019 Demini-%
from ED from Fees mus Change
Benzo(a)pyrene (Component of 83329/POMTV & 50-32-8 0.600720 0.703390 1.0 -14.6%
56553/7PAH)
Methylene di phenyl di isocyanate (MDI) (Componen IO 1-68-8 26.16 25.66 10.0 1.9%
83329/POMTV)
Naphthalene (Component of 83329/POMTV) 91 -20-3 11.35 13.25 1.0 -14.4%
Acetaldehyde 75-07-0 19,923.67 19,722.09 10.0 1.0%
Acetophenone 98-86-2 0.000370 0.000430 100.0 NIA
Acrolein 107-02-8 6,047.96 5,982.40 10.0 1.1%
Benzene 71-43-2 264.88 262.29 1.0 1.0%
Carbon tetrachloride 56-23-5 5.20 6.08 1.0 -14.6%
Chlorine 7782-50-5 9 1.23 106.82 100.0 -14.6%
Ch lorobenzene 108-90-7 3.81 4.46 10.0 -14.6%
Chloroform 67-66-3 3.23 3.79 100.0 -14.6%
Cumene 98-82-8 7,066.64 6,966.07 100.0 1.4%
DEHP (Di(2-ethylhexyl)phthalate) 117-81-7 0.054300 0.063600 10.0 -14.6%
Dichlorobenzene(p), 1,4-I 06-46-7 0.278800 0.260200 1.0 7.1%
Dinitro-o-cresol, 4,6-(& salts) 534-52-1 0.242500 0.284000 1.0 -14.6%
Dinitrophenol, 2,4-51-28-5 0.020800 0.024300 0.1 -14.4%
Dinitrotoluene, 2,4-121-14-2 0.108800 0.127400 0.1 -14.6%
Ethyl benzene 100-4 1-4 3.56 4.00 100.0 -11.1 %
Ethylene dichloride ( 1,2-dichloroethane) I 07-06-2 3.35 3.92 1.0 -14.6%
Formaldehyde 50-00-0 8,697.81 8,573.97 10.0 1.4%
Hexachlorobenzene 118-74-1 508.11 594.95 10.0 -14.6%
Hexane, n-110-54-3 389.02 356.11 100.0 9.2%
Hydrogen chloride (hydrochloric acid) 7647-01-0 392.63 459.74 100.0 -14.6%
MEK (methyl ethyl ketone, 2-butanone) 78-93-3 317.14 309.47 100.0 2.5%
Methanol (methyl alcohol) 67-56-1 57,255.42 56,697.46 1,000.0 1.0%
11/05/2021 Page 3 of 5
Largest Individual HAP Methanol (methyl alcohol) 57,255.42 lbs
Total HAP Emissions 11 9,065.57 lbs
Largest Individual CAP NOx ' 141.26 tons
Total CAP Emissions 460.71 tons
Total TAP Emissions 47,128.30 lbs
Total Aggregate 461.07 tons
Emissions
DAO's Comments Regarding Inventory
There were several pollutants with changes in emissions greater than I 0% and above the deminimis
value. Vinyl acetate emissions increased by 2 1.3% due to the increase in throughput on OS80 -Tech
Shield Adhesive. The propylene oxide emissions increased by 13.2% due to an increase in run
hours on the diesel fired emergency generator (OS20). Chromic acid (CrVI) increase was primarily
due to increased wood fuel consumption in the bark burner and an update to the emissions factor for
gas in the TOH's. The emissions for the following pollutants were most influenced by OS-86 (dryer
system with new RTO's -primary operating scenarios): Carbon monoxide (+14.3%), sulfur dioxide
(-22.4%), and the following pollutants with decreases from IO -14.6%: antimony, beryllium,
cadmium, cobalt, carbon tetrachloride, chlorine, chlorobenzene, mercury, benzo (a) pyrene,
naphthalene, carbon tetrachloride, chloroform, DEHP, dinitro-o-cresol, dinitrophenol, dini trotoluene,
ethyl benzene, ethylene dichloride, hexachlorobenzene, hydrogen chloride, methyl chloride, methyl
chloroform, nitrophenol, pentachlorophenol, perchloroethylene, propylene dichloride, selenium
compounds, TCE, trichlorobenzene, vinyl chloride. The throughput for OS-86 increased by 2.5% from
2019 to 2020. Changes in emissions are attributed the changes to the ratio of run time of different dryer
configurations in the primary operating mode and the change to the emission factor for gas in the
TOH's. Any additional information provided from the faci lity after the 11/5 submission, will be included in the
final packet. DLR.
11/05/2021 Page 5 of 5
~ac1llty total LY .lU.lU .l!,m1ss1on ~ummary Kecorctect ID .l!,U I
.I Facility Name: Louisiana-Pacific Corporation -Roxboro
Green House Gases Pollutants (GHG)
Pollutant CAS
CO2 equivalent (sum of individual OHO pollutant emissio1
times their 1995 JPCC Global Warming Potential (GWP),
converted to metric tons)
Criteria Pollutants
Pollutant CAS
co '2.SO~ co
NOx 2So~ NOx
PM(TSP) 250-~ TSP
PMl0 2'50.\v-.. PMI0
PM2.5 PM2.5
SO2 SO2
voe '2.50 ~ voe
Hazardous Air Pollutants (HAPs)
and/or Toxic Air Pollutants (TAPs)
Pollutant CAS
Antimony & Compounds (total mass, inc elemental SB)
Antimony Unlisted Compounds -Specify Compourn SBC-Other
(Component of SBC)
Arsenic & Compounds (total mass of elemental AS, arsine and
all inorganic compounds) \ o ·S '2. \\,
Arsenic Unlisted Compounds -Specify Compound A SC-Other
(Component of ASC)
Beryllium & compounds (Total mass) r1-s:z..\'o
Beryllium Metal (unreacted) (Component of BEC) 7440-41-7
Cadmium & compounds (total mass includes elemental metal)
1.-Vl..•~ \b
(\ '1 f") 0 I") f\") I
~ aclllty lU ff: / J UUUt) I
Permit #(s): 07760T24
Actual Emissions % Tons/Yr
Demini-Change
mus
Not Not NIA
Reported Reported
No GHGs ~.~ ..,~ ~
Reported voes'" t-> \\ l 0'-'·°' \."-"
Actual Emissions
(Tons/Year)
CY2020 CY2019 Demini-%
from ED from Fees mus Change
"'116.33 101.77 0.5 14.3%
,;-141.26 135.49 0.5 4.3%
✓ 68.10 66.30 0.5 2.7%
v 66.38 64.60 0.5 2.8%
66.38 64.60 0.5 2.8%
6.84 8.81 0.5 -22.4%
It/ 129.90 127.85 0.5 1.6%
Actual Emissions
(Pounds/Year)
CY2020 CY2019 Demini-%
from ED from Fees mus Change
1.82 2.14 10.0 , -15.0%
-
1.82 2.14 10.0 -14.6%
✓ 4.70 4.66 0.01 0.9%
4.70 4.66 0.01 0.9%
✓0.254230 0.297710 1.0 -14.6%
0.254230 0.297710 1.0 -14.6%
✓ 1.18 1.33 0.1 -11.3%
Pa11e 1 of :'i
E~111ty total LY .. m1.u Em1ss1on :summary Kecoraeu m 1<.,U
f
Facility Name: Louisiana-Pacific Corporation -Roxboro
Hazardous Air Pollutants (HAPs)
and/or Toxic Air Pollutants (TAPs)
Pollutant CAS
Benzo(a)pyrene (Component of 83329/POMTV & 50-32-8
56553/7PAH)
Methylene diphenyl diisocyanate (MDI) (Componen IO 1-68-8
83329/POMTV)
Naphthalene (Component of 83329/POMTV) 91-20-3
Acetaldehyde ✓ 75-07-0
Acetophenone ✓ 98-86-2
Acrolein ·✓ I q Cf 317101-02-8
Benzene ✓ 71-43-2
Carbon tetrachloride " 56-23-5
Chlorine 7782-50-5
Chlorobenzene ✓ I 08-90-7
Chloroform v 67-66-3
Cumene ✓ 98-82-8
DEHP (Di(2-ethylhexyl)phthalate) V 117-81-7
Dichlorobenzene(p ), 1,4-v I 06-46-7
Dinitro-o-cresol, 4,6-(& salts) V 534-52-1
Dinitrophenol, 2,4-v 51-28-5
Dinitrotoluene, 2,4-v 121-14-2
Ethyl benzene V 100-41-4
Ethylene dichloride ( 1,2-dichloroethane) V 107-06-2
Formaldehyde , L\"' s,5~-oo-o
Hexachlorobenzene \j 118-74-1
Hexane, n-✓ 110-54-3
Hydrogen chloride (hydrochloric acid) \ S~<\07i~7-0l-O
MEK (methyl ethyl ketone, 2-butanone) V 78-93-3
Methanol (methyl alcohol) ✓ 67-56-1
f\ '7 /'l O /'l f\"l I
I< aclllty IU ff: / JUUUt> l
Permit #(s): 07760T24
Actual Emissions
(Pounds/Year)
CY 2020 CY2019 Demini-%
from ED from Fees mus Change
r .....
0.600720 0.703390 1.0 I~,
26.16 25.66 10.0 1.9%
11.35 13.25 1.0 r 14.4%
19,923.67 19,722.09 10.0 1.0%
0.000370 0.000430 100.0 NIA
V, 6,047.96 5,982.40 10.0 1.1%
264.88 262.29 1.0 1.0%
5.20 > 6.08 1.0 -14.6% '
91.23 106.82 100.0 ~~ .
1 .....
3.81 4.46 10.0 ~'¼: C( .....
3.23 3.79 100.0 ~ :----.
7,066.64 6,966.07 100.0 1.4%
0.054300 0.063600 lO.O '[Jl~
0.278800 0.260200 1.0 7.1%
'~1~
,,...
0.242500 0.284000 1.0
0.020800 0.024300 0.1 i; *"¾'
0.108800 0.127400 0.1 -14.6%
3.56 4.00 100.0 -i-11 ----e -"';1 o/o-~
3.35 ...._ 3.92 1.0 -14.6%
I✓ 8,697.81 8,573.97 10.0 1.4%
508.11 594.95 10.0 -14.6%
389.02 356.11 100.0 9.2%
V 392.63 459.74 100.0 :r=t4.6%
317.14 309.47 100.0 2.5%
57,255.42 56,697.46 1,000.0 1.0%
ll,argest Individual HAP Methanol (methyl alcohol) 57,255.42 lbs
Total HAP Emissions 119,065.57 lbs
Largest Individual CAP NOx 141.26 tons
Total CAP Emissions 460.71 tons
Total TAP Emissions 47,128.30 lbs
Total Aggregate 461.07 tons
Emissions
DAO's Comments Regarding Inventory
f\'7 /,0 /,f\") I P::111e .'i of .'i
Reddix, Dawn
From:
Sent:
To:
Subject:
Ross,
Reddix, Dawn
Wednesday, November 3, 2021 1 :58 PM
Ross Reed
RE: [External] RE: Questions for call when we can reschedule or email response
I hope your processes have leveled out now. Sometimes it takes a while.
As far as the questions below, I do not need the 'map' for OS-63. I got that all figured out.
The only remaining question is in relation to the pollutants with changes greater than 10%. OS-86 was the main
contributor for all of the pollutants with changes greater than 10% that were not directly explained by
throughput. OS86 saw a 2.5% increase in throughput while SO2 decreased by 22.4%, CO increased by 14.3%, and the
rest of the pollutant emissions decreased between 10 -14.6%: antimony, beryllium, cadmium, cobalt, carbon
tetrachloride, chlorine, chlorobenzene, mercury, benzo (a) pyrene, naphthalene, carbon tetrachloride,
chloroform, DEHP, dinitro-o-cresol, dinitrophenol, dinitrotoluene, ethyl benzene, ethylene dichloride,
hexachlorobenzene, hydrogen chloride, methyl chloride, methyl chloroform, nitrophenol, pentachlorophenol,
perchloroethylene, propylene dichloride, selenium compounds, TCE, trichlorobenzene, vinyl chloride.
I believe you posed this question to the consultant. Once you hear back from him, let me know.
Thanks so much,
Dawn Reddix
From: Ross Reed [mailto:[e-mail]]
Sent: Monday, November 1, 2021 4:23 PM
To: Reddix, Dawn <[e-mail]>
Subject: [External] RE: Questions for call when we can reschedule or email response
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Dawn,
I believe the following information will clarify all but one item, which I am waiting on hearing back from the lead
consultant .
For OS-86 -New primary operating scenario with dryers, thermal oil heaters and RTO's. I have not been able to match
up emission factors with throughputs to give the emissions reported in AERO. One page has emission factors in
lb/mmbtu, but I failed to find any MMbtus for 2020. On the "Spreadsheet EMF" tab units are in lbs/mm BTU and
calculated to lb/year on the "Spreadsheet Emissions" tab. Emissions fact ors found on the "Spreadsheet EMF" tab are
from various sources ( i.e. AP-42, DAQ Emissions Calculator, NACASI, etc .... ) and tabulated on the "Spreadsheet
Emissions" tab. The other emission rate and subtotals are on tabs where emission rates are either specified in our
permit or testing at this or a similar LP mill. They are all totaled on the "Facility Emissions" tab.
1
Emissions tab), which adds 18.1 % to the emission rate of the single pass dryer emission rate. Note: The run time is a
total run t ime of all single pass dryers and the emission rate is the (Alternate Operating Scenario emission rate/ 4
(number of dryers run during testing)) * .181 which is added to the total of each criteria pollutant in OS-86.
Same goes for SO2. except it went down 22.4% in the same OS86. OS86 is Dryer system with new RTO's Primary
Operating Scenario. Correction: SO2 went down 22.4% for the overall facility but the vast majority of it came from
OS86. Many of the HAP changes dropped from 10 to 15% and is due almost exclusively from OS86. When I
reviewed the draft and ran through the QA/QC tools before the report was reported all the HAP/TAP %'s were within+/-
5% of last years. I've reached out to the senior consultant for clarification on this.
If you have any questions, please let me know. BTW we are still down struggling to get our line back up and going.
Thank you,
Ross
Ross C. Reed
Environmental Health & Safety Manager
10475 Boston Road
Roxboro, NC 27574
[e-mail]
T [phone]
C [phone]
LP Building Products
LPCorp.com
Louisiana-Pacific Corporation
From: Reddix, Dawn <[e-mail]>
Sent: Friday, October 29, 2021 3:31 PM
To: Ross Reed <[e-mail]>
Subject: Questions for call when we can reschedule or email response
Ross,
I hope that everything is well.
After going through your spreadsheet, I have the following unresolved questions/issues:
For OS-86 -New primary operating scenario with dryers, thermal oil heaters and RTO's. I have not been able to match
up emission factors with throughputs to give the emissions reported in AERO. One page has emission factors in
lb/mmbtu, but I failed to find any MMbtus for 2020.
3
intended recipient without the permission of the sender. If you are not the intended recipient of this message or their
agent, or if this message has been addressed to you in error, please immediately alert the sender by reply email and
thereafter permanently delete the message and any attachments.
5
Reddix, Dawn
From:
Sent:
To:
Subject:
Ross Reed <[e-mail]>
Monday, November 1, 2021 4:23 PM
Reddix, Dawn
[External] RE: Questions for call when we can reschedule or email response
CAUTION: External email. Do not click links or open attachments unless you verify. Send all suspicious email as an attachment to
Report Spam.
Dawn,
I believe the following information will clarify all but one item, which I am waiting on hearing back from the lead
consultant.
For OS-86 -New primary operating scenario with dryers, thermal oil heaters and RTO's. I have not been able to match
up emission factors with throughputs to give the emissions reported in AERO. One page has emission factors in
lb/mmbtu, but I failed to find any MMbtus for 2020. On the "Spreadsheet EMF" tab units are in lbs/mmBTU and
calculated to lb/year on the "Spreadsheet Emissions" tab. Emissions factors found on the "Spreadsheet EMF" tab are
from various sources ( i.e. AP-42, DAQ Emissions Calculator, NACASI, etc .... ) and tabulated on the "Spreadsheet
Emissions" tab. The other emission rate and subtotals are on tabs where emission rates are either specified in our
permit or testing at this or a similar LP mill. They are all totaled on the "Facility Emissions" tab.
-
For OS-87 -the only pollutant I have a question on is MDI -the emission factor is .000037 lb/MSF; the MSF is 510716;
.0000037*510716=18.896 lb MDI; the amount reported is 0.276 pounds. On tab "Stack Test Emission Factors", cell C33,
the emission factor is .000037 lbs/hr not lb/MSF; (.000037 lbs/hr)*(7,455.2 hr)= .2758 lbs/MDI.
For OS-63 -Pressing OSB -when I use the emission factors in the packet for Press, along with the board feet, I am not
getting the emissions reported. For this one, I need the map from the emission factors to the emissions. I will provide a
map if the screenshot below of the formula required by our permit does not clarify. When there have been questions in
the past it was due to the equation including (actual production rate)/ (tested production rate) which takes into account
the wide range of speeds we run for the various products. Let me know if you still want a map.
1
If you have any questions, please let me know. BTW we are still down struggling to get our line back up and going.
Thank you,
Ross
Ross G. Reed
Environmental Health & Safety Manager
10475 Boston Road
Roxboro, NC 27574
[e-mail]
T [phone]
C {336) 583-6876
LP Building Products
LPCorp.com
Louisiana-Pacific Corporation
From: Reddix, Dawn <[e-mail]>
Sent: Friday, October 29, 2021 3:31 PM
To: Ross Reed <[e-mail]>
Subject: Questions for call when we can reschedule or email response
• ~ "' I ~ -~ .,. > \ ' > • -' l
, . I ~
..--~ .. ''-" "' ' ~ ' ; . ... . ~ . -.
Ross,
I hope that everything is well.
After going through your spreadsheet, I have the following unresolved questions/issues:
For OS-86 -New primary operating scenario with dryers, thermal oil heaters and RTO's. I have not been able to match
up emission factors with throughputs to give the emissions reported in AERO. One page has emission factors in
lb/mmbtu, but I failed to find any MMbtus for 2020.
For 05-87 -the only pollutant I have a question on is MDI -the emission factor is .000037 lb/M5F; the M5F is 510716;
.0000037*510716=18.896 lb MDI; the amount reported is 0.276 pounds.
For 05-63 -Pressing O5B -when I use the emission factors in the packet for Press, along with the board feet, I am not
getting the emissions reported. For this one, I need the map from the emission factors to the emissions.
For OS-68 -Wax Storage -there are 2966076 lb/year throughput and O emissions.
3
Reddix, Dawn
From:
Sent:
To:
Ross Reed <[e-mail]>
Monday, November 1, 2021 11 :48 AM
Reddix, Dawn
Subject: RE: [External] RE: Questions for call when we can reschedule or email response
CAUTION: External email. Do not click links or open attachments unless you verify. Send all suspicious email as an attachment to
Report Spam.
I take you have worked in manufacturing?
From: Reddix, Dawn <[e-mail]>
Sent: Monday, November 1, 202111:46 AM
To: Ross Reed <[e-mail]>
Subject: RE: [External] RE: Questions for call when we can reschedule or email response
No worries. Ross. I am glad to know that you are well. Believe me, I understand process downtime and the struggle to
level out once you start back up. I hope that leveling out happens sooner rather than later. I do look forward to hearing
your responses on the inventory questions. End of day sounds great.
Thanks so much,
Dawn
From: Ross Reed [mailto:[e-mail]]
Sent: Monday, November 1, 202111:41 AM
To: Reddix, Dawn <[e-mail]>
Subject: [External] RE: Questions for call when we can reschedule or email response
CAUTION: External email. Do not click links or open attachments unless you verify. Send all suspicious email as an attachment to
Report Spam.
Dawn,
I apologize about Friday. We were down from Wednesday morning until early Saturday morning and have struggled
since. I'm starting to go through it and hope to have your questions answered by the end of the day.
Thank you,
Ross
From: Reddix, Dawn <[e-mail]>
Sent: Friday, October 29, 2021 3:31 PM
To: Ross Reed <[e-mail]>
Subject: Questions for call when we can reschedule or email response
1
To: Reddix, Dawn <[e-mail]>
Subject: [External) LP Roxobor AE1_2020 Draftl.xlsx
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thereafter permanently delete the message and any attachments.
3
Reddix, Dawn
From:
Sent:
To:
Subject:
Ross Reed <[e-mail]>
Monday, November 1, 2021 11 :41 AM
Reddix, Dawn
[External) RE: Questions for call when we can reschedule or email response
CAUTION: External email. Do not click links or open attachments unless you verify. Send all suspicious email as an attachment to
Report Spam.
Dawn,
I apologize about Friday. We were down from Wednesday morning until early Saturday morning and have struggled
since. I'm starting to go through it and hope to have your questions answered by the end of the day.
Thank you,
Ross
From: Reddix, Dawn <[e-mail]>
Sent: Friday, October 29, 2021 3:31 PM
To: Ross Reed <[e-mail]>
Subject: Questions for ca ll when we can reschedule or email response
Ross,
I hope that everyt hing is well.
After going through your spreadsheet, I have the following unresolved questions/issues:
For 05-86 -New primary operating scenario with dryers, thermal oil heaters and RTO's. I have not been able to match
up emission factors with throughput s to give the emissions reported in AERO. One page has emission factors in
lb/mmbtu, but I failed to find any MMbtus for 2020.
For OS-87 -the only pollutant I have a question on is MDI -the emission factor is .000037 lb/MSF; the MSF is 510716;
.0000037*510716=18.896 lb MDI; the amount reported is 0.276 pounds.
For OS-63 -Pressing OSB -when I use the emission factors in the packet for Press, along with the board feet, I am not
getting the emissions reported. For this one, I need the map from the emission factors to the emissions.
For 05-68 -Wax Storage -there are 2966076 lb/year throughput and O emissions.
Those are the only scenarios that I was unable to decipher. Your input will be great ly appreciated. The other thing that I
need some input on is explaining the emissions that changed by+/-10% last year that do not seem to be directly related
to throughput.
So far, this is what I 've found -Tons of wood burned in OS86 increased 2.5% to 356,200 t ons in 2020 from 347,592
tons in 2019. But, the CO difference was + 14.3% so there must be something else. Same goes for S02. except it
went down 22.4% in the same OS86. OS86 is Dryer system with new RTO's Primary Operating
l
Reddix, Dawn
From:
Sent:
To:
Subject:
Attachments:
Ross Reed <[e-mail]>
Wednesday, October 27, 2021 1 :44 PM
Reddix, Dawn
[External] LP Roxboro AE1_2020 Draft.xlsx
LP Roxobor AE1_2020 Draft.xlsx
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1
Reddix, Dawn
From:
Sent:
To:
Subject:
Attachments:
Ross Reed <[e-mail]>
Wednesday, October 27, 2021 1 :48 PM
Reddix, Dawn
[External] LP Roxobor AEI_2020 Draft1 .xlsx
LP Roxobor AEI_2020 Draft1 .xlsx
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1
Louisiana Pacific Roxboro's Air Emissions Inventory -Toxic Compliance 2020
Total
TPER In
Pollutant (lbllyr) TPER llmlt TPER llmlt 12nd) 2020 TPER Emlnlon• Compliance
Acetaldehyde 19,923.67 6.80 lb/hr 2.54 lb/hr yes
benzo (a)pyrene 0.601 2.20 lb/yr 0.6008 lb/yr yes
Carbon Tetrachloride 5.20 460 lb/vr 5.20 lb/yr yes
Chlorine 91.23 0.23 lb/hr 0.79 lb/day 0.28 lb/day yes
Chlorobenzene 3.81 46 lb/day 0.01 lb/day yes
Chloroform 3.23 290 lb/yr 3.23 lb/vr yes
di(2-ethy1hexvllohthalate 0.0543 0.63 lbs/day 0.00 lb/day yes
Ethvlene dichloride 3.3489 260.00 lb/yr 3.35 lb/yr yes
n-hexane 389.02 23.00 lbs/day 1.19 lb/day yes
Mercury, aryl and
inorganic compounds 0.86 0.013 lb/day 0.003 lb/dav yes
1, 1, 1-Trichloroethane 3.58 250 lb/day 64 lbs/hr 0.01 lb/day yes
Methyl ethyl ketone 317.14 22.4 lb/hr 78 lb/day 0.97 lb/day yes
methyl isobutyt ketone 788.61 7.6 lb/hr 52 lb/day 2.42 lb/day yes
Chloromethane 2.66 1600 lb/yr 0.39 lbs/hr 0.00 lb/hr yes
Nickel 21.13 0.13 lb/day 0.06 lb/day yes
Pentachlorophenol 0.006 0.0064 lb/hr 0.063 lbs/day 0.0000 lb/hr yes
Stvrene 444.13 2.70 lb/hr 1.43 lb/hr yes
TCDD-2378 4.66E-10 0.00020 lb/vr 0.0000 lb/vr yes
1oerchloroethylene 4.39 13000 lb/yr 4.39 lb/yr yes
Toluene 743.95 14.40 lb/hr 98 lb/day 2.28 lb/day yes
Trichloroethy1ene 3.46 4,000 lb/yr 3.46 lb/yr yes
V1nvt Chloride 2.08 26 lb/vr 2.08 lb/vr yes
Xylene 581.28 16.40 lb/hr 57 lb/day 1.87 lb/day yes
Dryer Dryer Insignificant Insignificant PF PF
RTO's RTO's RT0#3 RT0#3 Sources Sources CP002 CP002 CP003/ Tanks Tanks CP005 CP005 TechShiel TechShield
Pollutant Limit Actual Limit Actual Limit Actual Limit Actual CP003/4 Limit 4 Actual Limits Actual Limit Actual d Limit Actual'
Acrolein (lbs/hr) 20.32 0.62 2.44 0.16 NA NA NA NA NA NA
Arsenic (lbs/hr) 0.0012 0.0006 NA NA NA NA NA NA NA
Benzene (lbs/hr) 0.60 0.03 0.24 0.00 0.12 332.80 NA NA NA NA NA
Benzene (lbs/yrJ NA 332.80 0.12 NA NA NA NA NA
Beryllium Metal (lbs/hr) 0.02 0.00 NA NA NA NA NA NA NA
Cadmium Metal (lbs/hr) 0.03 0.00 NA NA NA NA NA NA NA
Chromium (VI) (lbs/hr) 0.00042 0.00010 NA NA NA NA NA NA NA
Formaldehyde (lbs/hr) 6.54 0.42 7.5 0.17 NA 1.9 0.42 0.16 0.05 0.27 0.00 0.095 0.029 0.27 0.0663
HydrOQen Chlonde (lb/hr) 182.54 0.05 NA NA NA NA NA NA NA
Manqanese (lbs/hr) 23.81 0.00 NA NA NA NA NA NA NA
Phenol (lbs/hrl 2.06 0.24 17.30 0.73 NA 0.79 0.08 NA 3.18 0.00 0.018 0.0011 NA
Permit No. 07760T23
LP Roxboro Facility ID: 7300061
Calendar Year
Hou"' of O,,.r1tlon
!Total Drver RTO's
Dryer RTO's (4-6) (POS)
Dryer RTO's (4-8\ /ADS)
Single Pass D,..,er
RT().3 / Press
B-1, B·2, B-3 B-5
B-8, B-7
B-8
T&G Production
!Teen Shield
F•ePun!>
EmerJleflCV Q8/lerator
Production Data -All Products . ·----~·-·· --~-~-·. ·----~-r-l>slll'
7/16 RS 4136
15/32 RS 42 6
1/2 RS
19/32 RS 41 3
Supersuuc BaslC 19/32 4200
23132 TN250 3924
23132 TN350 3825
23132 Leaacv 4165
Superstruc Bas,c 23/32 42 00
Superstrue A<lvan 23132 4500
Totals
Production Data -T&G .. ----~·-·· --~-·--
Tvoe
23132 TN250 I
23/32TN350 I
23/32 Leaacv I
Total TFP
Annual Average Production Rate
T1
All
TechShtefd
r2
All
Louisiana Pacific Roxboro's Air Emissions Inventory
User Input
2020
7,830.9
4 872 2
2,958 7
13 707 9
7 4552
74552
6 167 •
5,362 1
6,167.4
4 0299
218
11 1
B<I-FI (318 ,net,) TFP
301,629888 194 928 3
15,761,760 10,491.4
0.0
17611328 11,364.8
127 660 838
32 462 752 20,122.7
109 052,384 70,455.1
33,230,400 23,403.4
556416 3651
283360 1992
610,715,968 331,413.8
lbs.11" Board-Feet (3/8 Inch baSIS)
392 32 462,752
383 109,052,384
41 7 33,230,400
174,745,536
Board-Feet 1318 Inch bas,s:
68~505
Board-Feet (3/8 ,nch basis)
110,?510307
Usage Data
Hours of Bypass Total Mil Gas ConslXl1pllOn [Therms)
nn.er RTO's (4-8) CPOS\ oc Total Mitl Gas Consumpbon (mmsc:o
Dryer RTO's (4-6) (AOS) 00 !Dryer RTO's Gas Consumpbon (mmsc!)
RTO-3 00 Press RTO Gas Consumption (mmsc!)
Of)'ers 33 C ITOH's Gas Consumpt,on (mmsc:f\
WESPBvoass 33 C trota1 Wafer tlYouoh<l.rt lhrnuoh divers (tons)
Ba11t Burner Idle 5868 rwood Fuel consumed by Bal1t Bumer {tons)
POOi 392 Green Wood Fuel consumed by Bar1< Burner (tons)
CP003 060 Resonated Wood Fuel consumed bv Bark Burner (tons)
CP005 0""1 Wood Fuel consumed by TOH llons\
\,P006 o ,c Parts wasi-lluod
\,P007 01C Na• lne Ink U.,.,,.. '""'s)
:Pooe OH StellCll Paint and End Stnp {gals)
Nail Lme and s1enol
Slamp Ink (APA. Looo)
Ink Jel Ink and Cleaner
°""""' E"""seat (oats\
Grevs and Black Edaeseal (rudsl
Clear Edgeseal
Total Edaeseal Usace
TechShield Glue (gal)
M1stv Mean Green '!""'
PF ConsumpllOI\ {ll>s )
MDI Consumpl,on (lbs.)
TFP
19,903 7
651758
21,625 7
106,705,3
The cells ., red are user inp<rt Al other eels are arlh« calcllfaled values or ate const8/lts
LP Roxboro Facility ID: 7300061
216.1l
112 91
96 75
6~
356,271
116,301
115.877
430
6 511
0
67!\11
3 375
10,125
4 245
0
155 2!\11
18 900
12,150
186,300
178200
0
0
16.392 880
Permit No. 07760T24
Mr. Sarder
October J, 2019
Page4
ATTACHMENT to Penn.it No. 07760T23
Insil:mificant Activities per 15A NCAC 020 .0503(8)
Emission Source ID Emission Source Description No.
Edgeseal operation consisting of2 paint booths:
IS-E -1 one on the main tine, which also applies/sprays a logo and end
[MACT, DODD] strips; one on the T &G. End strips are also applied to the
product by water based aerosol cans just next to the spray
booth. (Group 1 miscellaneous coating onerations)
Printing operations consisting of the Logo and AP A stamp
operations and Re-grade. The AP A stamp goes on the saw line,
IS-P6 -I where the Logo goes on in the paint booth. Boards that fail
(MACT, DODD] quality standards required for AP A certification are re-graded
by covering the AP A stamp either manually with a ro1ler or a
spray system located between the saw line and stacker units'
(Group t miscellaneous coating ooerations)
IS~(;/}
rMACT, DDDDl paint spray booth (Group 1 miscellaneous coating operations)
IS-N-1 nail line marking (Group J miscellaneous coating operations) rMACf DDDDl
IS-SV-1 stencil painting or "end stripping" (Group 1 miscellaneous
[MACT, DODD] coating operations)
IS-Ikl diesel fuel tank
IS-G-1 gasoline fuel tank
IS-B-1 battery charging operation
IS-WC-I welding and cutting torch
IS-00-1 I)\ ~
~1~ two zep cleaning stations -degreaser drums (55 gallons)
IS-BC-1 blade cleaning operation
IS-HH-l hand held grinding equipment
IS-J>-£'-1 portable pump
IS-C0-1 compressor oil
IS-TO-1 thermal oiJ storage
IS-HO-I hydraulic oil storage reservoir
IS-HO-2 hydraulic oil system
IS-HO-3 hydraulic oil tank (19,800 gallons)
1s-rl 1 propane tank (1,500 pounds)
IS-DB-1 debarker
IS-W 2 waferizer
Regulation
15A NCAC 02Q
.0503(8)
1 Applicability Detennination 2760 received by DAQ on December 29, 20 t 5. Email response that same
day that no pe:nnit application was necessary.
Mr. Sarder
October I, 2019
Pages
Emission Source ID
No.
IS-CII'-1
1S-B$-1
IS-W-!{
IS-V0 -1
IS-W--1
IS-DF-1
[MACT, ZZZZ]
IS-WE-1 & IS-wt:-2
IS-MbI-3 & IS-Mro-4
IS-PF 5 & IS-PP-6
I-MO
fMACT. DDDDl
Emission Source Description
cutting torch
bench scale grinding
welder
used oil tank
wax tanks
diesel fire pump (275 bhp)
two volatile organic liquid storage tanks (12,000 gallon
capacity each)
one volatile organic liquid or soybean oil storage tank1 and one
volatile organic liquid storage tank, respectively (30,000 gallon
capacity each)
two volatile organic liquid storage tanks (15,000 gallon
capacity each)
mark-out system at the TechShreld® line (Group 1
miscellaneous coating ooerations)
Regulation
15A NCAC 02D
.0524, 40 CFR Part
60, Subflart 1111 is
not apf icable to
(IS-D -1/ because
the diese fi re Nu.mp pre-dates the
SPS re~ation
and 15A CAC 020 .0503(8)
15ANCAC02D
.0524, 40 CFR Part
60 -S u~part Kb
exempllons
October 15, 2003,
Federal Rister
~Volume 6 . No.
99) and 15A
NCAC 02Q
.0503(8)
15ANCAC02Q
.0503(8)
1. Because an activity is insignificant does not mean that the activity is exempted from an applicable requirement or
that the Permittee is exempted from demonstrating compliance with any applicable requirement.
2. When applicable, emissions from stationary source activities identified above shall be included in determining
compliance with the permit requirements for toxic air pollutants under 15A NCAC 020 . l 100 "Control ofToxic
Air PolJutants" or 02Q .071 I "Emission Rates Requiring a Permit".
3. For additional information regarding the applicability of MACT or GACT see the DAQ page titled "The
Regulatory Guide for Insignificant Activities/Permits Exempt Activities". The link to this site is as
follows: httJ)://deq.nc.gov/about/divisions/air--quality/air-quality-pennits/specific-pennit-conditions-
regulatory-guide.
"I.
Permit 07760T21
Page3
SECTION 1 -PERMITTED EMISSION SOURCE(S) AND ASSOCIATED AIR
POLLUTION CONTROL DEVICE(S) AND APPURTENANCES
The followinP. table contains a swnmarv of all permitted emission sow-ces and associated air r IJution conttol devices and annurtenances:
Emission
Source JD
No.
BARK.I
Dt l through
D-5
MACT
DODD
BAW<-1
MACT
DDDD
Emission Source Description
Wafer Drying Process
one bark/wood (dry and wet)-
fuel/recycled resinated wood
fuel1-fired burner (190 million
Btu per hour maximum heat input
rate) providing direct heat to five
triple-pass direct fired wafer
drvers2
Wafer Drying Process
one bark/wood (dry and wet)-
fuel/recycled resinated wood
fuel1-6red burner (190 million
Btu per hour maximum heat input
rate) providing heat to single-
pass direct fired wafer dryer
one bark/wood (dry and wet)-
fuel/recycled resinated wood
fuel 1-fired burner (190 million
Btu per hour maximum heat input
rate) providing heat to single-
pass direct fired wafer dryer2
one bark/wood (dry and wet)-
fuel/recycled resinated wood
fuel1-fired burner (190 million
Btu per hour maximum heat input
rate) providing heat to single-
pass direct fired wafer dryer2
one bark/wood ( dry and wet)-
fuel/recycJed resinated wood
fuel1-fired burner (190 million
Btu per hour maximum heat input
rate) providing heat to single-
pass direct fired wafer dryer
Control
Device
ID No.
PCYCD-1
through
PCYCD-5,
WESP-1,
WESP-2,
RT0-4,
RTQ..5 and
RTQ..6
PCYCD-1,
WESP-1,
WESP-2,
RT0-4,
RTO-5 and
RTO-6
PCYCD-2,
WESP-1,
WESP-2,
RTO-4,
RTO-5 and
RTO-6
PCYCD-3,
WESP-1,
WESP-2,
RTO-4,
RTO-5 and
RTO-6
PCYCD-4,
WESP-1,
WESP-2,
RTO-4,
RT0-5 and
RTO-6
Control Device Description
five cyclones (144 inches in diameter each)
installed one each on the dryers,
two wet electrostatic precipitators (22,651
square feet of collection area each), and
three propane/natural gas-fired
regenerative thermal oxidizers ( l 1. 0
million Btu oer hour heat input rate, each)
One cyclone (144 inches in diameter each)
installed on the dryer and in series with
two wet electrostatic precipitators (22,651
square feet of collection area each), and
three propane/natural gas-fired
regenerative thermal oxidizers ( l I. 0
million Btu per hour heat input rate, each)
One cyclone (144 inches in diameter each)
installed on the dryer and in series with
two wet electrostatic precipitators (22,651
square feet of collection area each), and
three propane/natural gas-fired
regenerative thermal oxidizers (11.0
million Bh1 oer hour heat input rate. each)
One cyclone (144 inches in diameter each)
installed on the dryer and in series with
two wet electrostatic precipitators (22,651
square feet of collection area each), and
three propane/natural gas-fired
regenerative thermal oxidizers (1 1.0
million Btu oer hour heat input rate each)
One cyclone (144 inches in diameter each)
installed on the dryer and in series with
two wet electrostatic precipitators (22,651
square feet of collection area each), and
three propane/natural gas-fired
regenerative thermal oxidizers (1 1.0
million Btu oer hour heat input rate, each)
Permit 07760T21
Page 4
Emission
Source ID
No.
3*0.5A
TQR-1
TOIJ-2
NSPS De;
MACT
DODD
TOH-1
TOH-2
.1109 Case-
by-Case
MACT;
MACT
DDDDD
C'{C9
CP-003 and
CP-004
CP-07
FUELPREP
Emission Source Description
one bark/wood (dry and wet)-
fuel/recycled resinated wood
fuel1-fired burner (190 million
Btu per hour maximum heat input
rate) providing heat to single-
pass direct fired wafer dryer
Primga_ O~ratin~ Scenario
(POS)
two wood fuel/recycled resinated
wood fueVnatural gas-fired
thermal oil heaters (40 million
Btu per hour heat input rate
each) exhausting directly to the
bark burner and indirectly
supplying heat to the presses
Alternate O~rating_ Scenario
fAOSJ
two wood fuel/recycled resinated
wood fuel/natural gas-fired
thermal oil heaters (40 million
Btu per hour heat input rate
each) exhausting to stacks (atm)
while firing natural gas onJv
saw trim recovery (screen)
cyclone (84 inches in diameter)
exhausting to CP-003
Fuel Pree Sl'.stem
raw fuel bin transfer and loading
system (high pressure blower)
sanderdust bin transfer and
loading system
metering bin transfer and
loading system
Control Control Device Description
Device
ID No.
PCYCD-5, One cyclone (144 inches in diameter each)
WESP-1, installed on the dryer and in series with
WESP-2, two wet electrostatic precipitators (22,651
RTO-4, square feet of collection area each), and
RTO-5 and three propane/natural gas-fired
RTO-6 regenerative thermal oxidizers ( l l. 0
million Btu oer hour heat input rate, each)
PCYCD-1 five cyclones (144 inches in diameter each)
through installed one each on the dryers,
PCYCD-5,
WESP-1 two wet electrostatic precipitators (22,651
and WE.SP-square feet of collection area each), and
2, and
RT0-4 three propane/natural gas-fired
through regenerative thermal oxidizers (I 1.0
RTO-6 million Btu per hour heat input rate, each)
NI A NIA
NIA NIA
B-3 and/ or one bagti.lter (2,21. 9 square feet of filter
CYC3 area) and/or one bypass cyclone (96 inches
in diameter)
B-7 one bag-filter ( 4 79 square feet of filter area)
B-8 and/or one bagfilter (2,219 square feet of filter
CYC8 area) and/or one bypass cyclone (84 inches
in diameter)
Pennit 07760T2 l
Page 5
Emission
Source ID
No.
CP-02
CPf /and CV 5
p -1 and R -
2
MACT
DODD
TS-l.fillH
and
TS-1.CO
MACT
0000
cP..bo1
CP .. 006
BljGl
MACT zzzz4
F-1
Emission Source Description
OSB forming proc~
blender and fonning bin
aspiration systems
mat reject and flying saw system
with bypass cyclone (120 inches
in diameter)
OSB board urocessin2
operation
two OSB press enclosure vents
from one totally enclosed hot
press
TechShield® Coating
Operation consisting of:
Adhesive roll coating operation
and associated sheathing
application
Cleaning operations
Eini~bio2 12m~~
sawtrim and finishing line clean-
up operation
tongue and groove and
sanderdust aspiration system
one diesel-fired emergency
generator (1,332 horsepower)
bark handling fugitives
Control Control Device Description
Device
JD No.
B-2 one bagfilter (2,219 square feet of filter
area)
B-5, and/or one bagfilter (5,235 square feet of filter
CYCS-2 area) and/or two bypass cyclones (120
(wet); or inches in diameter)
CYCS-1
(dry)
RTO-3 one propane/natural gas-fired regenerative
thermal oxidizer (24 million Btu per hour
heat input)
NIA NIA
B-1 and/or one bagfilter (5,235 square feet of filter
CYC1 area) and/or one bypass cyclone (120
inches in diameter)
B-6 and/or one bag.filter (3,698 square feet of filter
CYC6 area) and/or one bypass cyclone (96 inches
in diameter)
NIA NIA
NIA NIA
1 Per the application (7300061.08A) request and for the puiposc of CISWI NSPS applicabil~, the Permittee is allowed to only combust wood
and recycled rcsinated wood-waste that is not ~ified as a "solid wa~te" as of May 12, 2010, issuance of Pennit No. 07760Tl7.
2 Per email dated March 17, 2016 each dryer and ~iated process cyclone has an inlet airflow design of55,000 ACFM (275,000 ACFM
total) and each WESP has an inlet airflow design of 150,000 ACFM (300,000 ACFM total).
3 D-LA through D-5A are the replacement dryers for D-1 through D-5 (Application# 7300061.19A).
4 140 CFR § 63.6580, Subpart ZZZZ] per 63.6590(a)( l)(i) Stationary RICE located at a major source of HAP emissions, a stationary
RICE is existing if you commenced construction or reooostruction of the stationary RICE before December 19, 2002. Therefore, per
63.6590(b)(3) an existing emergency RICE does not have to meet the requirements of this subpart and of subpart A of this part. No initial
notification is necessary.
'
Mr. Sarder
December 8, 2020
Page4
A IT ACHMENT to Permit No. 07760T24
Insi1mificant Activities ner 15A NCAC 020 .0503(8)
Emission Source ID No. Emission Source Description
Edgeseal operation consistin_g of2 paint booths:
IS-EO-1
one on the main line, which also applies/sprays a logo and end
[MACT, DDDD] strips; one on the T &G. End strips are also applied to the
product by water based aerosol cans just next to the spray
booth. (Grouo 1 misceUaneous coating onerations)
Printing operations consisting of the Logo and APA stamp
operations and Re-grade. The AP A stamp goes on the saw line,
IS-P0-1
where the Logo goes on in the paint booth. Boards that fail
[MACT, DDDD] quality standards required for AP A certification are re-graded
by covering the AP A stamp either manually with a roller or a
spray system located between the saw line and stacker units1
(Grouo 1 miscellaneous coating onerations)
IS-C-1 paint spray booth (Group 1 miscellaneous coating operations) fMACT. DDDDl
IS-N-1 nail line marking (Group 1 miscellaneous coating operations) IMACT. DDDDl
IS-SP-1
[MACT, DDDD]
stencil painting or "end stripping" (Group 1 miscellaneous
coating operattons)
IS-D-1 diesel fuel tank
IS-G-1 gasoline fuel tank
IS-B-1 battery charging operation
IS-WC-l welding and cutting torch
IS-DD-1 two zep cleaning stations -degreaser drums (55 gallons)
IS-BC-1 blade cleaning operation
lS-HH-1 hand held grinding equipment
IS-PP-1 portable pump
IS-C0-1 compressor oil
JS-TO-1 thermal oil storage
IS-HO-1 hydraulic oil storage reservoir
IS-HO-2 hydraulic oil system
IS-HO-3 hydraulic oil tank (19,800 gallons)
IS-P-1 propane tank (1 ,500 pounds)
IS-DB-1 debarker
IS-W-2 waferizer
IS-CT-1 cutting torch
1 Applicability Determination 2760 received by DAQ on December 29, 2015. Email response that same
day that no permit application was necessary.
Mr. Sarder
December 8, 2020
Page 5
IS-BS-I
TS-W-3
JS-UO-1
IS-W-1
IS-DF-1
rMACT. ZZZZl
IS-WE-I & IS-WE-2
IS-MDI-3 & lS-MDI-4
IS-PF-5 & IS-PF-6
I-MO
rMACT. DDDDl
bench scale grinding
welder
used oil tank
wax tanks
diesel fire pump (275 bhp)
two volatile organic liquid storage tanks (12,000 gallon
capacity each)
one volatile organic liquid or soybean oil stor~e tank1 and one
volatile organic liquid storage tank. respective y (30,000 gallon
capacity each)
two volatile organic liqwd storage tanks (15,000 gallon
capacity each)
mark-out system at the TechShield line (Group l miscellaneous
coating ooerations)
1. Because an activity is insignificant does not mean that the activity is exempted from an applicable requirement or
that the Pennittee is exempted from demonstrating compliance with any applicable requirement.
2. When applicable, emissions from stationary source activities identified above shall be included in determining
compliance with the permit requirements for toxic air pollutants under I SA NCAC 02D . 1100 "Control of Toxic
Air Pollutants" or 02Q .0711 "Fmissi.on Rates Requiring a Permit".
3. For additional information regarding the applicability ofMACT or GACT see the DAQ page titled "The
Regulatory Guide for insignificant Activities/Pennits Exempt Activities". The link to this site is as
follows: http://deq.nc.gov/about/divisions/air-guality/air-guality-pennits/specific-permit-conditions-
regulatory-guide.
, Permit 07760T24
Page 3
SECTION 1 -PERMITTED EMISSION SOURCE(S) AND ASSOCIATED AIR
POLLUTION CONTROL DEVICE(S) AND APPURTENANCES
The followin11, table contains a swnmarv of all permitted emission sow-ces and associated air t >llutiou control devices and a :
Emission Emission Source Description Control Control Device Description
Source JD Device
No. JD No.
BARK.I Wafer Dn:in& Process PCYCD-1 Five cyclones (144 inches in diameter
MACT one bark/wood ( dry and wet)-through each) installed one each on the dryers,
DODD fuel/recycled resinated wood
fuel1-fired burner (190 miJlion
PCYCD-5,
Btu per hour maximum heat input WESP-1, Two wet electrostatic precipitators (22,65 I
rate) providing direct heat to five WESP-2, square feet of collection area each), and
triple-pass direct fired wafer RTO-4, three propane/natural gas-fired
dryers2 and providing heat RTO-5 and regenerative thermal oxidizers ( l 1.0
to five single-pass direct fired
wafer dryer2 (ID Nos. 3D-l
RTO-6 miJlion Btu per hour heat input rate, each)
through D-5 and D-lA through
D-SA)
TOH-1 Primar"l_ Operating_ Scenario PCYCD-1 Five cyclones ( 144 inches in diameter
TOH-2 (POS) through each) installed one each on the dryers,
NSPS Dc; Two wood fuel/recycled PCYCD-5,
MACT resinated wood fuel/natural gas-
DODD fired thermal oil heaters (40 WESP-1 Two wet electrostatic precipitators (22,651
million Btu per hour heat input and WESP-square feet of collection area each), and
rate each) exhausting directly to 2, and
the bark burner and indirectly
supplying heat to the presses RTO-4 Three propane/natural gas-fired
through regenerative thennal oxidizers (l J.O
RTO-6 million Btu per hour heat input rate, each)
TOH-1 Alternate Ooerating_ Scenario NI A NIA
TOH-2 (AOS)
MACT Two wood fuel/recycled
DDDDD resinated wood fuel/natural gas-
fired thermal oil heaters (40
mitJion Btu per hour heat input
rate each) exhausting to stacks
(atm) while firing natural gas
onlv
Pennit 07760T24
Page4
Emission
Source ID
No.
CYC9
CP-003 and
CP-004
CP-007
FUEL
PREP
CP-002
CP-005 and
CYC5
PV-l and PY-
2
MACT
DODD
TS-1.ADH
and
TS-1.CO
MACT
0000
Emission Source Description
saw trim recovery (screen)
cyclone (84 inches in diameter)
exhausting to CP-003
Fuel Prel! Sl:'.stem
raw fuel bin transfer and loading
system (high pressure blower)
sanderdust bin transfer and
loading system
metering bin transfer and
loading system
OSB forming l!rocess
blender and forming bin
aspiration systems
mat reject and flying
saw system with bypass
cyclone ( 120 inches in
diameter)
OSB board l!rO£essing
operation
Two OSB press enclosure vents
from one totally enclosed hot
press
TechShield® Coating O~ration
consisting of:
Adhesjve roll coating operation
and associated sheathing
application
Cleaning operations
Control Control Device Description
Device
1DNo.
NIA NIA
B-3 and/ or One bagfilter (2,219 square feet of filter
CYC3 area) and/or one bypass cyclone (96 inches
in diameter)
B-7 One bagfilter (479 square feet offiJter
area)
B-8 and/or One bagfilter (2,2 19 square feet of filter
CYC8 area) and/or one bypass cyclone (84 inches
in diameter)
B-2 One bagfilter (2,219 square feet of filter
area)
B-5, and/or One bagfilter (5,235 square feet of filter
CYC5-2 area) and/or two bypass cyclones ( 120
(wet); or inches in diameter)
CYC5-1
(dry)
RTO-3 One propane/natural gas-fired regenerative
thermal oxidizer (24 million Btu per hour
heat input)
NIA NIA
Pennjt 07760T24
Page 5
Emission
Source ID
No.
CP-001
CP-006
ENGl
MACT
ZZZZA
F-1
Emission Source Description
Finishing process
sawtrim and finishing line clean-
up operation
tongue and groove and
sanderdust aspiration system
One diesel-fired emergency
generator {1,332 horsepower)
bark handling fugjtives
Control ControlDe~ce Description
Device
1D No.
B-1 and/or One bagfilter (5,235 square feet of filter
CYCI area) and/or one bypass cyclone (120
inches in diameter)
B-6 and/or One bagfilter (3,698 square feet of filter
CYC6 area) and/or one bypass cycJone (96 inches
in diameter)
NIA NIA
NIA NIA
1 Per the application (7300061.08A) request and for the purpose of CISWT NSPS applicability, the Pcnnittee is allowed to only com bust
wood and recycled resinated wood-waste that is not classified as a "solid waste" as of May 12, 2010, issuance of Penn it No. 07760TI 7.
2 Per email dated March 17, 2016 each dryer and associated process cyclone has an inlet airflow design of55,000 ACFM (275,000 ACFM
total) and each WESP has an inlet airflow design of 150,000 ACFM (300,000 ACFM total).
3 O-IA through D-5A arc the replacement dryers for D-1 through 0-5 (Application # 7300061.19A).
4 l40 CFR § 63.6580, Subpart ZZZZ] per 63.6590(a)(])(i) Stationary RJCE located at a major source of HAP emissions, a stationary
RJCE is existing if you commenced construction or reconstruction of the stationary RICE before December 19, 2002. Therefore, per
63.6590(b)(3) an existing emergency RICE does not have to meet the requirements of this subpart and of subpart A of this part. No initial
notification is necessary.
Facility Name:
Facility ID:
Pollutant
OSID
Acetaldehyde
OS-20
OS-33
OS-63
OS-80
OS-86
Facility Emissions -Operating Scenarios Per Pollutant
Louisiana-Pacific Corporation -Roxboro
2020 Inventory
Louisiana-Pacific Corporation -Roxboro
7300061
Emission
Source ID
ENG i
IS-DF-1
PV-1
PV-2
TS-1.ADH
TS-I .CO
BARKI
BARKI.D-1
BARK 1.D-2
BARKI.D-3
BARKI.D-4
BARKI.D-4A
BARK I.D-5
TOH-I
TOH-2
Emission Rate -2020
0.002660 Pounds
0.032180 Pounds
I, 118.27 Pounds
89.59 Pounds
18,715.78 Pounds
Permit Number(s): 07760T24
ENGi
l S-DF-1
PV-1
PV-2
Emission Rate (Prev) -2019
0.024000 Pounds
0.052690 Pounds
1,096.77 Pounds
73.83 Pounds
TS-I.ADIi
TS-I.CO
I 8,551.42 Pounds
BARKI
BARK 1.D-I
BARKI.D-2
BARKI.D-3
BARKI.D-4
BARKI.D-4A
BARKI.D-5
TOH-I
TOH-2
TOTAL in C urrent Inventory: 19,923.67 Pounds TOTAL in Previous Inventory: 19,722.09 Pounds
Acetophenone
OS-86
7/29/2021
BARKI
BARK I.D-1
BARK I.D-2
BARKI.D-3
BARKI.D-4
BARKI.D-4A
0.000370 Pounds 0.000430 Pounds
BARKI
BARKI.D-1
BARKI.D-2
BARK I.D-3
BARK I.D-4
BARKI .D-4A
Page I of 31
Facility Name:
. Facility ID:
Pollutant
OS ID
OS-86
Louisiana-Pacific Corporation -Roxboro
7300061
Emission
Source ID
BARKI
BARK I.D-1
BARK.1.D-2
BARK l.D-3
BARKI.D-4
BARK 1.D-4A
BARK I.D-5
TOH-I
TOl l-2
Emission Rate -2020
4.70 Pounds
TOTAL in Current Inventory: 4.70 Pounds
Benzene
OS-20
OS-33
OS-63
OS-86
ENGi
IS-DF-1
PY-I
PY-2
BARKI
BARKI.D-1
BARK.1.D-2
BARKI.D-3
BARK.1.D-4
BARK.l.D-4A
BARK.1.D-5
TOIi-i
TOH-2
0.08 I 030 Pounds
0.039150 Pounds
29.82 Pounds
234.94 Pounds
TOTAL in Current Inventory: 264.88 Pounds
Benzo(a)pyrene (Component of 83329/POMTV & 56553/7PAH)
OS-63 0.000 I 20 Pounds
OS-86
7/29/2021
PY-I
PY-2
BARKI
BARK I.D-1
0.600600 Pounds
Permit Number(s): 07760T24
Emission Rate (Prev) -2019
4.66 Pounds
BARKI
BARKI .D-1
BARKI .D-2
BARKI .D-3
BARK I.D-4
BARKI.D-4A
BARK 1.D-5
TOH-I
TOH-2
TOTAL in Previous Inventory: 4.66 Pounds
ENGi
IS-DF-1
PY-I
PY-2
0.071500 Pounds
0.064120 Pounds
29.25 Pounds
232.90 Pounds
BARKI
BARKI.D-1
BARK 1.D-2
BARK I.D-3
BARKI.D-4
BARKI.D-4A
BARKI.D-5
TOH-I
TOH-2
TOTAL in Previous Inventory: 262.29 Pounds
PY-I
PY-2
0.000090 Pounds
0.703300 Pounds
BARKI
BARKI.D-1
Page 3 of3 I
Facility Name:
· Facility ID:
Pollutant
OS ID
Louisiana-Pacific Corporation -Roxboro
7300061
Emission
Source JD Emission Rate -2020
TOTAL in Current Inventory: 1.18 Pounds
Carbon tetrachloride
OS-86
BARK.I
BARKl.D-I
BARKI.D-2
BARK l.D-3
BARK 1.D-4
BARKI.D-4A
BARKI.D-5
TOH-I
TOH-2
5.20 Pounds
TOTAL in Current Inventory: 5.20 Pounds
Chlorine
OS-86
BARK!
BARKI.D-1
BARKI.D-2
BARKI.D-3
BARK 1.D-4
BARK 1.D-4A
BARK 1.D-5
TOH-I
TOH-2
91.23 Pounds
TOTAL in C urrent Inventory: 91.23 Pounds
Chlorobcnzene
OS-86
BARKI
BARKI .D-1
BA RKI.D-2
BARKI.D-3
BARK 1.D-4
BARKI.D-4A
BARKI.D-5
TOH-I
TOll-2
3.81 Pounds
TOTAL in Current Inventory: 3.81 Pounds
7/29/2021
Permit Number(s): 07760T24
Emission Rate (Prev) -2019
TOTAL in Previous Inventory: 1.33 Pounds
6.08 Pounds
BARKI
BARKI.D-1
BARKI.D-2
BARKI.D-3
BARK I .D-4
BARKI.D-4A
BARKI.D-5
TOH-I
TOH-2
TOTAL in Previous Inventory: 6.08 Pounds
I 06.82 Pounds
BARKI
BARK l.D-1
BARKl.0-2
BARKI.D-3
BARK l.D-4
BARKI.D-4A
BARKI.D-5
TOH-I
TOH-2
TOTAL in Previous Inventory: 106.82 Pounds
4.46 Pounds
BARKI
BARK 1.D-1
BARKI.D-2
BARKl.0-3
BARK l.D-4
BARKI.D-4A
BARK 1.D-5
TOH-I
TOl-l-2
TOTAL in Previous Inventory: 4.46 Pounds
Page 5 of3 I
Facility Name:
· Facility ID:
Pollutant
OS ID
Louisiana-Pacific Corporation -Roxboro
7300061
Emission
Source ID Emission Rate -2020
TOTAL in Current Inventory: 13.86 Pounds
co
OS-20
OS-33
OS-63
OS-86
E GI
IS-DF-1
PV-1
PV-2
BARK!
BARKI .D-1
BARKI.D-2
BARK I.D-3
BARK I.D-4
BARKI.D-4A
BARKI.D-5
TOH-I
TOH-2
0.040000 Tons
0.020000 Tons
5.58 Tons
110.69 Tons
TOTAL in C urrent Inventory: 116.33 Tons
Cobalt Unlisted Compounds -Specify Compound (Component of C
OS-86 1.60 Pounds
BARKI
BARKl.D-1
BARK I.D-2
BARKI.D-3
BARKI.D-4
BA RKI .D-4A
BARK 1.D-5
TOH-I
TOH-2
TOTAL in Current Inventory: 1.60 Pounds
Cumene
OS-63
7/29/2021
PV-1
PV-2
5, I 07.16 Pounds
Permit Number(s): 07760T24
Emission Rate (Prev) -2019
TOTAL in Previous Inventory: 13.73 Pounds
ENGi
IS-DF-1
PV-1
PV-2
0.040000 Tons
0.030000 Tons
5.52 Tons
96.18 Terns
BARK!
BARK I.D-1
BARK I.D-2
BARK I.D-3
BARKI.D-4
BARKI.D-4A
BARKI.D-5
TOH-I
TOH-2
TOTAL in Previous Inventory: 101.77 Tons
1.86 Pounds
BARK!
BARK l.D-1
BARK!.D-2
BARKI.D-3
BARKI .D-4
BARKI .D-4A
BARKI .D-5
TOH-I
TOH-2
TOTAL in Previous Inventory: 1.86 Pounds
PV-1
PV-2
5,054.31 Pounds
Page 7 of 3 1
Facility Name:
· Facility ID:
Pollutant
OS ID
Louisiana-Pacific Corporation -Roxboro
7300061
Emission
Source ID Emission Rate -2020
Dinitro-o-cresol, 4,6-(& salts)
OS-86
BARKI
BARK I.D-1
BARK 1.D-2
BARK I.D-3
BARK 1.D-4
BARK I.D-4A
BARK 1.D-5
TOH-I
TOH-2
0.242500 Pounds
TOTAL in Current Inventory: 0.24 Pounds
Dinitrophenol, 2,4-
OS-86
BARK I
BARKI.D-I
BARKI.D-2
BARKI.D-3
BARK I.D-4
BARK I.D-4A
BARKI .D-5
TOH-I
TOH-2
0.020800 Pounds
TOTAL in C urrent Inventory: 0.02 Pounds
Dinitrotoluene, 2,4-
OS-86
BARKI
BARKI.D-I
BARKI.D-2
BARKI .D-3
BARKI .D-4
BARK I .D-4A
BARKI.D-5
TOH-I
TOH-2
0.1 08800 Pounds
TOTAL in C urrent Inventory: 0.11 Pounds
Ethyl benzene
7/29/202 1
Permit Number(s): 07760T24
Emission Rate (Prev) -2019
0.284000 Pounds
BARK I
BARKI.D-1
BARK I.D-2
BARK I.D-3
BARKI.D-4
BARK 1.D-4A
BARK I.D-5
TOH-I
TOH-2
TOTAL in Previous Inventory: 0.28 Pounds
0.024300 Pounds
BARKI
BARK I.D-I
BARKI.D-2
BARKI.D-3
BARK I.D-4
BARK I.D-4A
BARKI.D-5
TOH-I
TOH-2
TOTAL in Previous Inventory: 0.02 Pounds
0.127400 Pounds
BARKI
BARKI .D-I
BARK I.D-2
BA RKI .D-3
BARKI .D-4
BARKI.D-4A
BA RKl .O-5
TOH-I
TOH-2
TOTAL in Previo us Inventory: 0.13 Pounds
Page 9 of3 I
Facility Name:
· Facility ID:
Pollutant
OSID
OS-80
OS-84
OS-86
OS-87
Louisiana-Pacific Corporation -Roxboro
7300061
Emission
Source ID
PV-1
PV-2
TS-1.ADH
TS-I.CO
CP-003
CP-004
CYC9
BAR.Kl
BARK l.D-1
BARKI.D-2
BARKI.D-3
BARK l.D-4
BARKI.D-4A
BARK l.D-5
TOH-I
TOH-2
CP-005
CYC5
Emission Rate -2020
267 .19 Pounds
40 I . I I Pounds
3,289.45 Pounds
214.50 Pounds
TOTAL in Current Inventory: 8,697.81 Pounds
Hexachlorobenzene
OS-86
BARK I
BARK 1.0-1
BARKI.D-2
BARKI.D-3
BARK l.D-4
BARKI.D-4A
BARK l.D-5
TOH-I
TOH-2
508.11 Pounds
TOTAL in Current Inventory: 508.11 Pounds
Hexane, n-
OS-63 174. 15 Pounds
7/29/2021
Permit Number(s): 07760T24
Emission Rate (Prev) -2019
PV-1
PV-2
220.19 Pounds
TS-1.ADH
TS-I.CO
CP-003
CP-004
CYC9
396.96 Pounds
3,261.40 Pounds
BAR.Kl
BAR.K I.D-1
BARKI.D-2
BARKI.D-3
BARK I.D-4
BARKI .D-4A
BARK l.D-5
TOH-I
TOH-2
CP-005
CYC5
212.28 Pounds
TOTAL in Previous Inventory: 8,573.97 Pounds
594.95 Pounds
BAR.Kl
BARK 1.D-1
BARKI.D-2
BARKI.D-3
BARKI.D-4
BARK I .D-4.A
BARK I .D-5
TOH-I
TOH-2
TOTAL in Previous Inventory: 594.95 Pounds
133.65 Pounds
Page 11 of3 I
Facility Name:
· Facility ID:
Pollutant
OS ID
Louisiana-Pacific Corporation -Roxboro
7300061
Emission
Source ID Emission Rate -2020
TOTAL in Current Inventory: 4.70 Pounds
Manganese Unlisted Compounds -Specify Compound (Component
OS-33 0.000250 Pounds
OS-63
OS-86
IS-DF-I
PV-1
PV-2
BARK!
BARKI .D-I
BARK I.D-2
BARKI.D-3
BARK I.D-4
BARKI.D-4A
BARK 1.D-5
TOH-I
TOH-2
0.036800 Pounds
21.93 Pounds
TOTAL in Current Inventory: 21.97 Pounds
MEK (methyl ethyl ketone, 2-butanone)
OS-86 3 17 .14 Pounds
BARKI
BARKI.D-I
BARKI.D-2
BARKI.D-3
BARKI.D-4
BARKI.D-4A
BARKI .D-5
TOH-I
TOH-2
TOTAL in Cur rent Inventory: 3 I 7.14 Pounds
Mercury, vapor (Component of HGC)
OS-33 0.000130 Pounds
OS-63
7/29/2021
IS-DF-I
PV-1
PV-2
0.025200 Pounds
Permit Number(s): 07760T24
Emission Rate (Prev) -201 9
TOTAL in Previous Inventory: 4.66 Pounds
IS-DF-I
PV-1
PV-2
0.000410 Pounds
0.028200 Pounds
21. 74 Pounds
BARK!
BARKI.D-I
BARK I.D-2
BARK I.D-3
BARKI.D-4
BARKI.D-4A
BARK I.D-5
TOH-I
TOH-2
TOTAL in Previous Inventory: 21.77 Pounds
309.47 Pounds
BARKI
BARKI.D-1
BARK I.D-2
BARK I .D-3
BARKI.D-4
BARKI.D-4A
BARK I.D-5
TOH-I
TOH-2
TOTAL in Previous Inventory: 309.47 Pounds
IS-DF-I
PV-1
PV-2
0.000210 Pounds
0.019300 Pounds
Page 13 of3 I
Facility Name:
· Facility 10:
Louisiana-Pacific Corporation -Roxboro
7300061
Pollutant
0 S 1O Emission
Source ID
TOH-2
Emission Rate -2020
TOTAL in C urrent Inventory: 57,255.42 Pounds
Methyl bromide (bromomethane)
OS-63
OS-86
PV-1
PV-2
BARKI
BARKI.D-1
BARK I.D-2
BARKI.D-3
BARKI.D-4
BARKI.D-4A
BARKI.D-5
TOH-I
TOH-2
204.29 Pounds
1.73 Pounds
TOTAL in Current Inventory: 206.02 Pounds
Methyl chloride (chloromethane)
OS-86
BARK!
BARKI.D-1
BARKI.D-2
BARK I.D-3
BARKI.D-4
BARKI.D-4A
BARKI.D-5
TOI i-i
TOH-2
2.66 Pounds
TOTAL in Current Inventory: 2.66 Pounds
Methyl chloroform
OS-86
7/29/2021
BARK.I
BARKI.D-1
BARKI.D-2
BARKI.D-3
BARK I.D-4
BARKI.D-4A
3.58 Pounds
Permit Number(s): 07760T24
Emission Rate (Prev) -2019
TOH-2
TOTAL in Previous Inventory: 56,697.46 Pounds
PV-1
PV-2
202.17 Pounds
2.03 Pounds
BARKI
BARKI.D-1
BARK I.D-2
BARK I.D-3
BARKI.D-4
BARKI.D-4A
BARKI.D-5
TOH-I
TOH-2
TOTAL in Previous Inventory: 204.20 Pounds
3.1 1 Pounds
BARKI
BARKI.D-1
BARK I.D-2
BARKI.D-3
BARKI.D-4
BARKI .D-4A
BARKI .D-5
TOH-I
TOH-2
TOTAL in Previous Inventory: 3.11 Pounds
4.19 Pounds
BARK!
BARKI.D-1
BARK 1.D-2
BARK I.D-3
BARKI.D-4
BA RKI.D-4A
Page 15 of 31
Facility Name:
· Facility ID:
Pollutant
OS ID
OS-86
Louisiana-Pacific Corporation -Roxboro
730006 1
Emission
Source ID
PV-2
BARK!
BARKI.D-I
BARK I.D-2
BARKI.D-3
BARKI.D-4
BARK I.D-4A
BARKI.D-5
TOH-I
TOH-2
Emission Rate -2020
277 .89 Pounds
TOTAL in Current Inventory: 788.61 Pounds
Naphthalene (Component of83329/POMTV)
OS-20 0.013320 Pounds
OS-33
OS-63
OS-86
ENGi
IS-OF-I
PV-1
PV-2
BARKI
BARKI.D-1
BARKI.D-2
BARK.1.D-3
BARKI.D-4
BARKI.D-4A
BARKI.D-5
TOH-I
TOH-2
0.003560 Pounds
0.059000 Pounds
11.27 Pounds
TOTAL in Current Inventory: 11.35 Pounds
Nickel metal (Component ofNIC)
OS-33
IS-OF-I
OS-63
PV-1
7/29/2021
0.000130 Pounds
0.203200 Pounds
Permit Number(s): 07760T24
Emission Rate (Prev) -2019
PV-2
271.12 Pounds
BARKI
BARK 1.0-1
BARKI.D-2
BARK 1.0-3
BARKI.D-4
BARK I.D-4A
BARKI.D-5
TOH-I
TOH-2
TOTAL in Previous Inventory: 776.55 Pounds
ENGi
IS-OF-I
PV-1
PV-2
0.011800 Pounds
0.005830 Pounds
0.045300 Pounds
13.19 Pounds
BARKI
BARK 1.D-1
BARKI.D-2
BARK 1.0-3
BARK 1.0-4
BARK 1.D-4A
BARK 1.0-5
TOH-I
TOH-2
TOTAL in Previous Inventory: 13.25 Pounds
0.000210 Pounds
IS-DF-1
0.155900 Pounds
PV-1
Page 17 of31
Facility Name:
. Facility ID:
Pollutant
OS ID
Louisiana-Pacific Corporation -Roxboro
7300061
Emission
Source ID
BARKI.D-4
BARKI.D-4A
BARKI .D-5
TOH-I
TOil-2
Emission Rate -2020
TOTAL in C urrent Inventory: 141.26 Tons
PC B (polychlorinated biphenyls)
OS-86
BARKI
BARKl.0-1
BARK I.D-2
BARKI.D-3
BA RKI .D-4
BARKI.D-4A
BARKl.0-5
TOH-I
TOH-2
0.001400 Pounds
TOTAL in C urrent Inventory: 0.00 Pounds
Pentachlorophenol
OS-86
BARK!
BARKI.D-1
BARK I.D-2
BARKI.D-3
BARK 1.D-4
BARKI.D-4A
BARK I.D-5
TOIi-i
TOH-2
0.005900 Pounds
TOTAL in Current Inventory: 0.01 Pounds
Perch loroethylene (tetrach loroethylene)
OS-86 4.39 Pounds
BARKI
BARK I.D-1
BARK I.D-2
BARKI.D-3
BARK I.D-4
BARKI.D-4A
7/29/2021
Permit Number(s): 07760T24
Emission Rate (Prev) -2019
BARK I.D-4
BARKI.D-4A
BARKI .D-5
TOH-I
TOH-2
TOTAL in Previous Inventory: 135.49 Tons
0.001600 Pounds
BARKI
BARK 1.0-1
BARKl .0-2
BARK I .D-3
BARKI.0 -4
BARKI.D-4A
BARKI.D-5
TOH-I
TOH-2
TOTAL in Previous Inventory: 0.00 Pounds
0.006600 Pounds
BARKI
BARK 1.0-1
BARK 1.0 -2
BARK I.D-3
BARK 1.0-4
BARK I.D-4A
BARK I.D-5
TOH-I
TOH-2
TOTAL in Previous Inventory: 0.01 Po unds
5. 14 Pounds
BARK!
BARK I.D-1
BARK I.D-2
BARK 1.D-3
BARK I.D-4
BARK 1.D-4A
Page I 9 of 31
Facility Name:
· Facility ID:
Pollutant
OSID
OS-2 1
OS-33
OS-59
OS-60
OS-63
OS-70
OS-77
OS-84
OS-86
OS-87
Louisiana-Pacific Corporation -Roxbo ro
7300061
Emission
Source ID
F-1
IS-DF-1
CP-006
FUELPREP
PV-1
PV-2
CP-00 1
IS-EO-1
CP-003
CP-004
CYC9
BARKI
BARKI.D-1
BARKI.D-2
BARK l.D-3
BARKI.D-4
BARKI .D-4A
BARK I.D-5
TOH-I
TOH-2
C P-005
CYC5
Emission Rate -2020
2.23 Tons
0.0 I 0000 Tons
3.27 Tons
1.77 Tons
20.45 Tons
4.40 Tons
1.16 Tons
2.20 Tons
29.90 Tons
0.480000 Tons
TOTAL in Current Inventory: 68.10 Tons
PMIO
OS-2 2.16 Tons
7/29/2021
Permit Number(s): 07760T24
Emission Rate (Prev) -2019
2.21 Tons
F-1
0.0 I 0000 Tons
IS-DF-1
3.56 Tons
CP-006
1.93 Tons
FUELPREP
PV-1
PV-2
CP-001
IS-EO-1
CP-003
CP-004
CYC9
20.23 Tons
4.31 Tons
1.25 Tons
2.16 Tons
27.96 Tons
BARKI
BARKI.D-1
BARKI .D-2
BARKI.D-3
BARKI.D-4
BARKI.D-4A
BARKI.D-5
TOH-I
TOH-2
0.480000 Tons
CP-005
CYC5
TOTAL in Previous Inventory: 66.30 Tons
2.12 Tons
Page2I of3I
Facility Name:
· Facility ID:
Pollutant
OSID
OS-87
Louisiana-Pacific Corporation -Roxboro
7300061
Emission
Source ID
CP-005
CYC5
Emission Rate -2020
0.480000 Tons
TOTAL in Current Inventory: 66.38 Tons
PM2.S
OS-2 2.16 Tons
CP-002
OS-7 0.060000 Tons
CP-007
OS-20 0.0 l 0000 Tons
ENG i
OS-2 1 0.780000 Tons
F-1
OS-33 0.0 I 0000 Tons
IS-DF-1
OS-59 3.27 Tons
CP-006
OS-60 1.77 Tons
FUELPREP
OS-63 20.45 Tons
PV-1
PV-2
OS-70 4.40 Tons
CP-001
OS-77 I. 16 Tons
IS-EO-1
OS-84 2.20 Tons
CP-003
CP-004
CYC9
OS-86 29.63 Tons
BARKI
BARKI.D-1
7/29/2021
Permit Number(s): 07760T24
Emission Rate (Prev) -2019
CP-005
CYC5
0.480000 Tons
TOTAL in Previous Inventory: 64.60 Tons
2.12 Tons
CP-002
0.070000 Tons
CP-007
0.0 I 0000 Tons
E G I
0. 780000 Tons
F-1
0.010000 Tons
IS-OF-I
3.56 Tons
CP-006
1.93 Tons
FUELPREP
20.23 Tons
PV-1
PV-2
4.31 Tons
CP-001
1.25 Tons
IS-EO-1
2.16 Tons
CP-003
CP-004
C YC9
27.69 Tons
BARK!
BARKl.D-1
Page 23 of 3 1
Facility Name:
· Facility 10:
PoUutant
0S10
Louisiana-Pacific Corporation -Roxboro
7300061
Emission
Source IO
BARKI.D-1
BARKI.D-2
BARKI.D-3
BARKI.D-4
BARKI.D-4A
BARKI.D-5
TOH-I
TOH-2
Emission Rate -2020
TOTAL in Current Inventory: 5,969.65 Pounds
Propylene dichloride (1 ,2-dichloropropane)
OS-86 3.81 Pounds
BARKI
BARKI.D-1
BARKI.D-2
BARK 1.0-3
BARK 1.0-4
BARKI.D-4A
BARK 1.0-5
TOIi-i
TOll-2
TOTAL in Current Inventory: 3.81 Pounds
Propylene oxide
OS-20
ENGi
0.288600 Pounds
TOTAL in Current Inventory: 0.29 Pounds
Selenium Com pounds
OS-33
OS-86
7/29/2021
IS-OF-I
BARKI
BARKI.D-1
BARK 1.0-2
BARK 1.0-3
BARKI.D-4
BARK 1.D-4A
BARK I.D-5
TOH-I
0.000630 Pounds
0.650000 Pounds
Permit Number(s): 07760T24
Emission Rate (Prev) -2019
BARKI.D-1
BARKl.O-2
BARKI.D-3
BARK 1.0-4
BARKI.O-4A
BARKI.D-5
TOH-I
TOH-2
TOTAL in Previous Inventory: 5,904.77 Pounds
4.46 Pounds
BARKI
BARKI.D-1
BARK 1.0-2
BARKI.D-3
BARK I.D-4
BARK I.D-4A
BARKI.D-5
TOH-I
TOH-2
TOTAL in Previous Inventory: 4.46 Pounds
0.255000 Pounds
ENGi
TOTAL in Previous Inventory: 0.26 Pounds
0.00 I 030 Pounds
IS-DF-1
0. 760000 Pounds
BARK!
BARKI.D-1
BARKI.D-2
BARKI.D-3
BARK 1.0-4
BARK I.D-4A
BARKI.D-5
TOH-I
Page 25 of3 I
Facility Name:
· Facility ID:
Pollutant
0S10
Louisiana-Pacific Corporation -Roxboro
7300061
Emission
Source ID Emission Rate -2020
TCE: (trichloroethylene)
OS-86
BARKI
BARKI.D-1
BARK l.D-2
BARK l.D-3
BARKI.D-4
BARKI.D-4A
BARK l.D-5
TOH-I
TOH-2
3.46 Pounds
TOTAL in Current Inventory: 3.46 Pounds
Toluene
OS-20
OS-33
OS-63
OS-86
ENG i
IS-DF-1
PV-1
PV-2
BARKI
BARKI .D-1
BARKI.D-2
BARK I.D-3
BARK I.D-4
BARKI.D-4A
BARKI.D-5
TOH-I
TOll-2
0.028860 Pounds
0.017160 Pounds
I 99.51 Pounds
544.39 Pounds
TOTAL in Current Inventory: 743.95 Pounds
Trichlorobenzene, 1,2,4-
OS-86
7/29/2021
BARKI
BARKI.D-1
BARK I.D-2
BARK 1.D-3
0.037100 Pounds
Permit Number(s): 07760T24
Emission Rate (Prev) -2019
4.06 Pounds
BARKI
BARK I.D-1
BARKI.D-2
BARK I.D-3
BARK 1.0-4
BARK I.D-4A
BARK I.D-5
TOIi-i
TOH-2
TOTAL in Previous Inventory: 4.06 Pounds
ENG i
IS-DF-1
PV-1
PV-2
0.025500 Pounds
0.028110 Pounds
197.37 Pounds
541.44 Pounds
BARKI
BARKI.D-1
BARK I.D-2
BARK 1.D-3
BARK l.D-4
BARK 1.D-4A
BARKI.D-5
TOH-I
TOH-2
TOTAL in Previous Inventory: 738.86 Pounds
0.043400 Pounds
BARK!
BARK l.D-1
BARK l.D-2
BARKI.D-3
Page 27 of3 I
Facility Name: Louisiana-Pacific Corporation -Roxboro
Facility ID: 7300061 Permit Number(s): 07760T24
Pollutant
OSID Emission
Source ID Emission Rate -2020 Emission Rate (Prev) -2019
OS-2 51.07 Tons 50.08 Tons
CP-002 CP-002
OS-7 0.560000 Tons 0.610000 Tons
CP-007 CP-007
OS-20 0.010000 Tons 0.0 I 0000 Tons
ENG i ENG i
OS-33 0.0 I 0000 Tons 0.0 I 0000 Tons
1S-DF-1 IS-DF-1
OS-59 5.03 Tons 5.47 Tons
CP-006 CP-006
OS-60 12.68 Tons 13.85 Tons
FUELPREP FUELPREP
OS-63 4.65 Tons 4.60 Tons
PV-1 PV-1
PV-2 PV-2
OS-70 9.10 Tons 8.92 Tons
CP-001 CP-001
OS-77 0.240000 Tons 0.260000 Tons
IS-EO-1 IS-EO-1
OS-78 0.100000 Tons 0.220000 Tons
IS-PO-I IS-PO-I
OS-80 1.10 Tons 0.900000 Tons
TS-1.ADH TS-1.ADH
TS-I.CO TS-I.CO
OS-84 9.10 Tons 8.92 Tons
CP-003 CP-003
CP-004 CP-004
CYC9 CYC9
OS-85 0.010000 Tons 0.020000 Tons
IS-B-1 IS-B-1
IS-BC-I IS-BC-I
IS-BS-I IS-BS-I
IS-C-1 IS-C-1
IS-CO-I IS-CO-I
7/29/2021 Page 29 of3 I
Facility Name:
. Facility ID:
Pollutant
OSID
OS-86
Louisiana-Pacific Corporation -Roxboro
7300061
Emission
Source ID
PV-1
PV-2
BARK !
BA RK l.0-1
BARK 1.0-2
BA RK I.D-3
BA RKI.D-4
BARKI.0-4A
BA RK l.D-5
TOH-I
TOH-2
Emission Rate -2020
356.53 Pounds
TOTAL in Current Inventory: 581.28 Pounds
7/29/2021
Permit Number(s): 07760T24
Emission Rate (Prev) -2019
PV-1
PV-2
348.13 Pounds
BARKI
BARK I.D-1
BARK 1.0-2
BARKI.D-3
BARKI.D-4
BARK 1.D-4A
BARKl.0-5
TOH-I
TOH-2
TOTAL in Previous Inventory: 570.55 Pounds
Page 31 of31
COPY of RECORD Date Submitted: 6/\()/202111:27:35
NC Dept ofEnvlronmentaf((uallty
Inventory Certification Form(Title V)
Facility Name: Louisiana-Pacific Corporation -Roxboro AUG 2 2021
104 7 5 Boston Road
Roxboro, NC 27574 Raleigh Regional Office
North Carolina Department of Environmental Quality
Division of Air Q uality
Facility ID : 7300061
Permit: 07760
County : Person
DAQ Region : RRO
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
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,Miehttel-Sa. det · Ge ,'/ ~,,. <
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 pennit and either
i. the facilities employ more than 250 persons or have gross annual sales or expenditures exceeding $25 rnillion(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 proprietorship; a general partner or the proprietor, respectively;
3. For a municipality, state, federal, or other public agency includes the chief executive officer having responsibility for the
overall operations ofa principal geographic unit of the agency (e.g., a Regional Administrator of EPA).
CERTIFlCATION STATEMENT: "' --~ ~:·
(!mnortant: Lei:all)'. Resnonsible Official, r~ad and sit;tn after all ssil!missi2ns are final.)
I certify that I am the responsible official for this facility1 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 ofup 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: /,, -30-2 oz 1
Printed Name: Mieh&lil ~ardeu c,.,, t Ht>n•, <,
Signature: L ~, • 1-lr ... ti. -A
' This form applies to Title V facilities. If this facility is not classified asTitle V, please telephone your regional office Emission
Inventory Contact at once for proper _forms.
I :,
6 ""f, /1,,,h t. (!? l1 c..,, /· C. o ......
Email address of Responsible Official: ,Mil,e.~areer@li,eor1uioffl I.fl
Information on this Form cannot be held confidential
COPY of RECORD Date Submitted: 6/30/2021 11:27:35
1
Wafer Drying Process -single-pass t 1 Quality BARKI.D-NC Dept of Environmen a direct fired wafer dryer [MACT 2A DDDD]
cyclone (144 ~sin ~~t)'.cyclon~ (144
inches in diameter),cyclone (144 mches m
diarneter),cyclone ( 144 i~ches in QffMt
diarnet~}e~(]WgdOiUlll !!),wet
electrostatic precipitator (22,651 square feet of PCYCD-1, collection area),wet electrostatic precipitator PCYCD-2, Wafer Drying Process -triple pass
CS-17 (22,651 square feet of collection . PCYCD-4, WESP-BARK.1.D-3 direct-fired wafer dryer [MACT area),propane/natural gas-fired regenerative 1, WESP-2, RT0-4, DDDD) thermal oxidizer (13.5 million Btu per hour RT0-5, RT0-6 heat input rate),propane/natural gas-fired
regenerative thermal oxidizer (13.5 million Btu
per hour beat input rate),propane/natural gas-
fired regenerative thermal oxidizer (13.5
million Btu per hour beat input rate),
BARK.l.D-Wafer Drying Process -single-pass
direct fired wafer dryer [MACT 3A DODD)
cyclone (144 inches in diameter),cyclone (144
inches in diameter),cyclone (144 inches in
diameter),cyclone (144 inches in
diameter),cyclone (144 inches in diameter),wet
electrostatic precipitator (22,651 square feet of PCYCD-1, collection area),wet electrostatic precipitator PCYCD-2, Wafer Drying Process -triple pass
CS-17 (22,651 square feel of collection PCYCD-4, WESP-BARK.1.D-4 direct-fired wafer dryer [MACT area),propane/natural gas-fired regenerative I, WESP-2, RT0-4, DODD] thermal oxidizer ( 13.5 million Btu per hour RT0-5, RT0-6 heat input rate),propane/natural gas-fired
regenerative thermal oxidizer (13.5 million Btu
per hour heat input rate),propane/natural gas-
fired regenerative thermal oxidizer (13.5
million Btu per hour heat input rate),
cyclone (144 inches in diameter),cyclone (144
inches in diameter),cyclone (144 inches in
diameter),cyclone (144 inches in
diameter),cyclone (144 inches in diameter),wet
electrostatic precipitator (22,651 square feet of PCYCD-1, collection area),wet electrostatic precipitator PCYCD-2, BARKI.D-Wafer Drying Process -single-pass
CS-17 (22,651 square feet of collection . PCYCD-4, WESP-direct fired wafer dryer [MACT area),propane/natural gas-fired regenerative 1, WESP-2, RT0-4, 4A DODD] thermal oxidizer (13.5 million Btu per hour RT0-5, RT0-6 beat input rate ),propane/natural gas-fired
regenerative thennal oxidizer (13.5 million Btu
per hour heat input rate),propane/natural gas-
fired regenerative thermal oxidizer (13.5
million Btu per hour heat input rate),
cyclone (144 inches in diameter)'.cyclon_e (144
inches in diarneter),cyclone (144 mcbes m
diameter),cyclone (144 inches in
diarneter),cyclone (144 inches in diameter),wet
electrostatic precipitator (22,651 square feet of PCYCD-1, collection area),wet electrostatic precipitator PCYCD-2, Wafer Drying Process -triple pass
CS-17 (22,651 square feet of collection . PCYCD-4, WESP-BARKI.D-5 direct-fired wafer dryer [MACT area),propane/natural gas-fired regenerative I, WESP-2, RT0-4, DODD] thermal oxidizer ( 13.5 million Btu per hour RT0-5, RT0-6 heat input rate),propane/natural gas-fired
regenerative thermal oxidizer (13.5 million Btu
per hour heat input rate),propane/natural gas-
fired regenerative thermal oxidizer (13.5
million Btu per hour heat input rate),
BARK.LO-Wafer Drying Process -single-pass
direct fired wafer dryer (MACT 5A DDDD)
3
IS-MDI-4 volatile organic liquid storage tank
(30,000 gallon capacity)
nail line marking (Group l
IS-N-1 miscellaneous coating operations)
[MACTDDDD)
IS-P-1 propane tank (1,500 pounds)
IS-PF-5 volatile organic liquid storage tank
(15,000 gallon capacity)
IS-PF-6 volatile organic liquid storage tank
(15,000 gallon capacity)
Printing operations consisting of the
Logo and AP A stamp operations and
Re-grade. The AP A stamp goes on
the saw line, where the Logo goes on
in the paint booth. Boards that fail
IS-PO-I quality standards required for APA
certification are re-graded by
covering the AP A stamp either
manually with a roller or a spray
system located between the saw line
and stacker units (Group I
miscellaneous coating operations)
IS-PP-I portable pump
stencil painting or "end stripping"
IS-SP-I (Group I miscellaneous coating
operations) [MACT DODD]
IS-TO-1 thennal oil storage
IS-UO-1 used oil tank
IS-W-1 wax tanks
IS-W-2 waferizer
IS-W-3 welder
IS-WC-I welding and cutting torch
IS-WE-I volatile organic liquid storage tank
(12,000 gallon capacity)
IS-WE-2 volatile organic liquid storage tank
(12,000 gallon capacity)
OSB board processing operation -propane/natural gas-fired regenerative thermal OSB press enclosure vent from one CS-I I oxidizers (24 million Btu per hour heat input RTO-3 PV-1 totally enclosed hot press [MACT rate) DODD]
OSB board processing operation -propane/natural gas-fired regenerative ~henna! OSB press enclosure vent from one CS-I I oxidizers (24 million Btu per hour heat input RTO-3 PV-2 totally enclosed hot press [MACT rate) DODD)
cyclone (144 inches in diameter),cyclone (144
inches in diameter),cyclone (144 inches in Wafer Drying Process -wood diameter),cyclone (144 inches in fuel/recycled resinated wood diameter),cyclone (144 inches in diameter),wet fuel/natural gas-fired thermal oil electrostatic precipitator (22,651 square feet of PCYCD-1, heater (40 million Btu per hour heat collection area),wet electrostatic precipitator PCYCD-2, input rate) -[POS) exhausting
CS-17 (22,651 square feet of collection . PCYCD-4, WESP-TOH-I directly to the bark burner and area),propane/natural gas-fired regenerative I, WESP-2, RTO-4, indirectly supplying heat to the thermal oxidizer (13.5 million Btu per hour RTO-5, RTO-6 presses [NSPS De, MACT DODD]; heat input rate),propane/natural gas-fired [AOS] exhausting to stacks (atm) regenerative thennal oxidizer (13.5 million Btu while firing natural gas only [MACT per hour heat input rate),propane/natural gas-DDDDD] fired regenerative thermal oxidizer (13.5
million Btu per hour heat input rate),
5
COPY of RECORD Date Submitted: 6/30/202111:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Roxboro, NC 27574
Emission Source & Operating Scenario List -See Instructions
.. ES Group ID .. ES ID
ORI TS-I.CO, TS-l.ADH
GR5 CP-005, CYC5
BARK.I, BARKl.O-1,
BARKI.D-2, BARKl.O-3,
G-56 BARK.l.D4, BARKI.D-
4A, BARK.l.D-5, TOH-I,
TOH-2
G-58 CP-003, CP-004, CYC9
G-62 IS-MDI4, IS-MDI-3
G-63 IS-PF-5, IS-PF-6
G-67 PV-1 , PV-2
IS-CO-I, IS-CT-I, IS-D-1,
IS-DD-la, IS-G-1, IS-HH-1,
IS-HO-I, IS-HO-3, IS-PP-I,
G-74 IS-TO-I, lS-UO-1, IS-B-1,
lS-BC-1, IS-BS-I, IS-C-1,
IS-DB-I, IS-HO-2, IS-N-1,
IS-P-1, IS-SP-I, IS-DD-lb,
IS-W-2, lS-W-3, IS-WC-I
BARKI.D-IA
BARKI.D-2A
BARK.l.D-3A
BARK.l.D-5A
CP-001
CP-002
CP-006
CP-007
ENGi
F-1
FUELPREP
IS-DF-1
IS-EO-1
IS-PO-I
IS-W-1
.. osm
79
80
87
86
84
61
62
63
85
NONE
NONE
NONE
NONE
70
2
59
7
20
21
60
33
77
78
NONE
Facility ID : 7300061
Permit : 07760
County : Person
DAQ Region : RRO
• OS Description
TechShield Cleanners
TechShield Adhesive
CP00-5, Mat reject and flying cutoff saw.
B-5, CYC5-l, CYC5-2, and CYC5
Dryer system with new RTO's Primary
Operating Scenario
Saw line baghouse and dryer screen fines
collection
Storage of MDI raw materials
Storage of phenol-formaldehyde resin raw
materials
Pressing OSB
Nail line and Stencil
NONE
NONE
NONE
NONE
sawtrim and finishing line clean-up with
bypass cyclone
blender and forming bin aspiration systems
Sander dust collection from tongue and
groove process
sanderdust bin transfer and loading system
diesel-fired emergency generator (1,332
horsepower)
bark handling fugitives
Wood fuel metering bin collection
diesel fire pump
Application of edgeseal to the finished
product.
Stamp ink
NONE
7
COPY of RECORD Date Submitted: 6/30/202111:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Roxboro, NC 27574
North Carolina Department of Environmental Quality
Division of Air Quality
Facility ID : 7300061
Permit: 07760
County : Person
DAQ Region : RRO
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
1. Emission Source ID (from permit)
or Emission Source Group ID
2. Emission Source Description :
3. Operating Scenario ID/
Description:
Group GR! consisting ofTS-1.CO, TS-1.ADH
TechShield
OS -79ff echShield Cleanners
4. SCC Number/Description: 49099998/Miscellaneous Volatile Organic Compound Evaporation; Identify
the Process and Solvent in Comments
5. Throughput/units in 2020:
(e.g. production or fuel use):
6. Fuel Information
(lf fuel is used)
7. Capture E fficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
8. Control Device Information : one
Order CS-ID CD ID
(as listed in permit)
I H~• Co,o~, I
(Btu/units)
Control Device Description
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
(in feet) Circle (enter If): (F) (Feel/sec) Rate (Acfm) Rectangle (L x W)
(in 0.1 feet)
T-IC FUGITIVE (NO 1 72 Area = I STACK)
ERP Description
TechShield Cleaner
9
COPY of RECORD Date Submitted: 6/30/202111:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Roxboro, NC 27574
North Carolina Department of Environmental Quality
Division of Air Quality
Facility ID : 7300061
Permit: 07760
County : Person
DAQ Region : RRO
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
1. Emission Source ID (from permit)
or Emission Source Group ID
2. Emission Source Description :
3. Operating Scenario ID/
Description:
Group GRl consisting ofTS-1.CO, TS-1.ADH
TechShield
OS -80ff echShield Adhesive
4. SCC Number/Description: 49099998/Miscellaneous Volatile Organic Compound Evaporation; Identify
the Process and Solvent in Comments
5. Throughput/units in 2020:
(e.g. production or fuel use):
6. Fuel Information
(If fuel is used)
7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
8. Control Device Information :None
Order CS-ID CDlD
178200 GAL/yr
%Sulfur
(as listed in permit)
%Ash Heat Content
(Btu/units)
Control Device Description
9. Emission Release Point (ERP) information: (Sources vented to more than one ERP use additional entry lines):
ERPID ERP Type Height Diameter Temperature Velocity Volume Flow
(in feet) Circle (enter#): (F) (Feet/sec) Rate (Adm) Rectangle (L x W)
{in 0.1 feet)
T-1 FUGITIVE (NO 1 72 Area = I STACK)
ERP Description
Fugitive emissions
from ahesive
11
COPY of RECORD DatelSU19mMt'tl~nw;jt)m~1 11:27:35
As entered in Afllll{j 2021
Facility Name: Louisiana-Pacific co·rporation -Roxboro
10475 Boston Road
Raleigh Regional OfficeFacility ID: 7300061
Permit: 07760
County : Person Roxboro, NC 27574 DAQ Region : RRO
North Carolina Department of Environmental Quality 1 Qua\\t)'
Division of Air Quality f£nvitonfl'enta
Air Pollutant Point Source Emissions Inventory -Ca~P}far 2020
1. Emission Source ID (from permit)
or Emission Source Group ID
2. Emission Source Description :
3. Operating Scenario ID/
Description:
4. SCC Number/Description:
5. Throughput/units in 2020:
(e.g. production or fuel use):
6. Fuel Information
(If fuel is used)
7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
8. Control Device Information :None
Order CS-ID CDID
Group GR5 consisting of CP-005, CYC5
OSB forming process -mat reject and flyin
OS -87/CP00-5, Mat reject and flying cutoff saw. B-5, CYC5-1, CYC5-
2, and CYC5
30700803/Sawmill Operations ; Sawdust Pile Handling
7455.2 HR/yr
%Sulfur %Ash Heat Content
(Btu/units)
Control Device Description
(as listed in permit)
9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):
ERPID 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)
circular stack for
VERTICAL CP00S STACK 43 4.8 75 31.5 34200.63 mat reject line and
saw system
13
COPY of RECORD Date Submitted: 6/30/202111:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Facility ID : 7300061
Permit: 07760
County : Person Roxboro, NC 27574
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
1. Emission Source ID (from permit)
or Emission Source Group ID
2. Emission Source Description :
3. Operating Scenario ID/
Description:
4. sec Number/Description:
5. Throughput/units in 2020:
(e.g. production or fuel use):
6. Fuel Information
(If fuel is used)
7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
8. Control Device Information :
Order CS-ID CDID
Group G-56 consisting ofBARK.l, BARK.l.D-1, BARK.l.D-2,
BARK.1.D-3, BARK.l.D-4, BARK.I .D-4A, BARK.1 .D-5, TOH-1, TOH-2
One bark burner, five natural gas fired dryers and two wood-fired
thermal heaters
OS -86/Dryer system with new RTO's Primary Operating Scenario
30701020/Oriented Strandboard (OSB) Manufacture; Direct Natural Gas-
fired Rotary Dryer, Hardwoods
356270 TON/yr
%Sulfur %Ash Heat Content
(Btu/units)
100
Control Device Description
(as listed in permit)
1 CS-17 PCYCD-1 One cyclone (144 inches in diameter)
2 CS-17 PCYCD-2 One cyclone (144 inches in diameter)
3 CS-17 PCYCD-4 One cyclone (144 inches in diameter)
4 CS-17 WESP-1 One wet electrostatic precipitator (22,65 1 square feet of collection
area)
5 CS-17 WESP-2 One wet electrostatic precipitator (22,65 1 square feet of collection
area)
6 CS-17 RTO-4 One propane/natural gas-fired regenerative thermal oxidizer (11
million Btu per hour heat input rate)
7 CS-17 RTO-5 One propane/natural gas-fired regenerative thermal oxidizer (11
million Btu per hour heat input rate)
8 CS-17 RTO-6 One propane/natural gas-fired regenerative thermal oxidizer ( 11
million Btu per hour heat input rate)
15
Operating Scenario: OS -86 Emission Source/Group ID: G-56
9. EmJssion Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):
ERPlD 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)
Dryer VERTICAL l 10 9.5 250 64.66 275000 DryerRTO
RTO STACK common stack
17
Cadmium Metal
( elemental unreacted, 7440-43-9 1.0782 08 AFTER
Component of CDC)
Carbon tetrachloride 56-23-5 5.1 966 08 AFTER
Chlorine 7782-50-5 91 .2296 08 AFTER
Chlorobenzene 108-90-7 3.8109 08 AFTER
Chloroform 67-66-3 3.2335 08 AFTER
Chromic acid (VI}
(Component of SolCR6 & 7738-94-5 0.8084 04 AFTER
CRC)
Chromium Unlisted CRC-Compounds (Specify & Other 13.862 04 AFTER
Component of CRC)
Cobalt Unlisted COC-Compound (Specify & Other 1.6015 08 AFTER
Component of COC)
Cumene 98-82-8 1959.48 08 AFTER
Di(2-ethylhexyl)phthalate 117-81-7 0.0543 08 AFTER
(DEHP)
Dichlorobenzene(p), 1,4-106-46-7 0.1627 08 AFTER
Dinitro-o-cresol, 4,6-( & 534-52-1 0.2425 08 AFTER
salts)
Dinitrophenol, 2,4-51-28-5 0.0208 08 AFTER
Dinitrotoluene, 2,4-121-14-2 0.1088 08 AFTER
Ethyl benzene 100-41-4 3.5559 08 AFTER
Ethylene dichloride (1,2-107-06-2 3.3489 08 AFTER
dichloroethane)
Formaldehyde 50-00-0 3289.45 04 AFTER
Hexachlorobenzene 118-74-1 508.11 08 AFTER
Hexane, n-110-54-3 214.866 08 AFTER
Hydrogen chloride 7647-01-0 392.6335 08 AFTER
(hydrochloric acid)
Lead Unlisted Compounds
(Specify and Component PBC-Other 4.6985 04 AFTER
of PBC)
Manganese Unlisted MNC-Compounds (Specify & Other 21.9289 04 AFTER
Component of MNC)
Mercury, vapor 7439-97-6 0.8394 08 AFTER
(Component of HGC)
Methanol 67-56-1 3288.97 04 AFTER
Methyl bromide 74-83-9 1.73 08 AFTER
Methyl chloride 74-87-3 2.6561 08 AFTER
Methyl chloroform 71-55-6 3.5799 08 AFTER
Methyl ethyl ketone 78-93-3 317.14 04 AFTER
Methyl isobutyl ketone 108-10-1 277.89 08 AFTER
Methylene chloride 75-09-2 33.4893 08 AFTER
Naphthalene (Component 91-20-3 11.2744 08 AFTER
of POMTV)
Nickel metal (Component 7440-02-0 20.922 04 AFTER
ofNIC)
Nitrophenol, 4-100-02-7 0.0127 08 AFTER
Pentachlorophenol 87-86-5 0.0059 08 AFTER
Perchloroethylene 127-18-4 4.3883 08 AFTER
(tetrachloroethylene)
Phenol 108-95-2 1879.43 04 AFTER
19
COPY of RECORD Date Submitted: 6/30/202111:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Facility ID : 7300061
Permit: 07760
County : Person Roxboro, NC 27574
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
1. Emission Source ID (from permit)
or Emission Source Group ID
2. Emission Source Description :
3. Operating Scenario ID/
Description:
4. SCC Number/Description:
5. Throughput/units in 2020:
(e.g. production or fuel use):
6. Fuel Information
(If fuel is used)
7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
8. Control Device Information :
Order CS-ID CD ID
Group G-58 consisting of CP-003, CP-004, CYC9
CP-003 raw fuel bin loading transfer system with bypass cyclone
OS -84/Saw line baghouse and dryer screen fines collection
30700710/Plywood Operations ; Sawing
7455.2 HR/yr
%Sulfur %Ash Heat Content
(Btu/units)
Control Device Description
(as listed in permit)
One bagfilter (2,219 square feet of filter area) 1 CS-6 B-3
9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle (enter#): (F) (Feet/sec) Rate (Acfm) Rectangle (L x W)
(in 0.1 feet)
circular stack for
VERTICAL CP003 28 3.8 75 19.4 13201.09 fuel bin transfer
STACK and loading system
21
COPY of RECORD Date Submitted: 6/30/202111:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Facility ID : 7300061
Permit : 07760
County : Person Roxboro, NC 27574
DAQ R egion : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory -Calendar Yea r 2020
1. Emission Source ID (from permit)
or Emission Source Group ID
2. Emission Source Description :
3. Operating Scenario ID/
Description:
4. SCC Number/Description:
5. Throughput/units in 2020:
(e.g. production or fuel use):
6. Fuel Information
(If fuel is used)
7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
8. Control Device Information :None
Order CS-ID CDID
Group G-62 consisting ofIS-MDI-4, IS-MDI-3
diphenylmethane-diisocyanate storage tanks
OS -61 /Storage of MDI raw materials
4078640 I/Pressure Tanks -Isocyanates ; Methyl Isocyanate: Withdrawal
Loss
16392880 LB/yr
I He>t eoo•mt I
(Btu/units)
Control Device Description
(as listed in permit)
9. Emission Release Point (ERP) [nformation: (Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feel) Cu'Clc (enter#): (F) (Feet/sec) Rate (Ad m) Rectangle (L x W)
(in 0.1 feet)
erp-fug FUGITIVE (NO 1 72 Area = 1 ERP for Fugitive
STACK) sources
23
COPY of RECORD Date Submitted: 6/30/202111:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Facility ID : 7300061
Permit: 07760
County : Person Roxboro, NC 27574
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
1. Emission Source ID (from permit)
or Emission Source Group ID
2. Emission Source Description :
3. Operating Scenario ID/
Description:
4. SCC Number/Description:
5. Throughput/units in 2020:
(e.g. production or fuel use):
6. Fuel Information
(If fuel is used)
7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
8. Control Device Information :None
Order CS-w CDID
Group G-63 consisting ofIS-PF-5, IS-PF-6
phenol-formaldehyde resin storage tanks
OS -62/Storage of phenol-formaldehyde resin raw materials
40788403/Pressure Tanks -Phenols ; Phenol: Withdrawal Loss
6424106 LB/yr
I H~t Conunt I
(Btu/units)
Control Device Description
(as listed in permit)
9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle (enter#): (F) (Feet/sec) Rate (Acfm) Rectangle (L x W)
(in 0.1 feet)
erp-fug FUGITIVE (NO 1 72 Area = 1 ERP for Fugitive
STACK) sources
25
COPY of RECORD Date Submitted: 6/30/202111:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Facility ID : 7300061
Permit : 07760
County : Person Roxboro, NC 27574
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
1. Emission Source ID (from permit)
or Emission Source Group ID
2. Emission Source Description :
3. Operating Scenario ID/
Description:
4. SCC Number/Description:
5. Throughput/units in 2020:
(e.g. production or fuel use):
6. Fuel Information
(lf fuel is used)
7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
8. Control Device Information :
Order CS-ID CDID
Group G-67 consisting of PV-1, PV-2
OSB press vents
OS -63/Pressing OSB
30701053/Oriented Strandboard (OSB) Manufacture ; Hot Press, Phenol-
Formaldehyde Resin
5 10715968 BDFT/yr
I H~, Coore"' I
(Btu/umts)
100
Control Device Description
(as listed in permit)
I CS-11 RTO-3 One propane/natural gas-fired regenerative thermal oxidizer (24
million Btu per hour heat input rate)
9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle (eotcr #): (F) (Feet/sec) Rate (A<fm) Rectangle (L x W)
in 0.1 feet)
erp-VERTICAL 60 3 72 5 2121 erp for thermal
TOH STACK oxidizers
27
Manganese Unlisted MNC-Compounds (Specify & Other 0.0368 08 66 AFTER
Component of MNC)
Mercury,vapor 7439-97-6 0.0252 08 0 AFTER (Component of HGC)
Methanol 67-56-1 1301.06 04 94 AFTER
Methyl bromide 74-83-9 204.29 08 90 AFTER
Methyl isobutyl ketone 108-10-1 510.72 04 95 AFTER
Methylene chloride 75-09-2 183.8577 08 90 AFTER
Methylene diphenyl
diisocyanate (MDI) 101-68-8 4.995 04 95 AFTER
(Component of POMTV)
Naphthalene (Component 91-20-3 0.059 09 95 AFTER ofPOMTV)
Nickel metal (Component 7440-02-0 0.2032 08 0 AFTER ofNIC)
Phenol 108-95-2 5464.661 04 95 AFTER
Polycyclic Organic Matter
(Inc PAH, dioxins, etc. NC POM 0.0639 09 95 AFTER & AP 42 historic
amorphous glob)
Propionaldehyde 123-38-6 11 92.82 04 95 AFTER
Styrene 100-42-5 224.72 08 90 AFTER
Toluene 108-88-3 199.5082 09 95 AFTER
Xylene 1330-20-7 224.715 08 90 AFTER
29
Operating Scenario: OS -85 Emission Source/Group ID: G-74
10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2020)
Hours per Day ( 22 ) Days per Week ( 7 ) Weeks per Year ( 50 )
11. Typical Start & End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throughput:
Jan-Feb + Dec
2020 25% March-May
2020 24% une-Aug.
2020 27% ept.-Nov.
2020
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions-Emission Control GHG CAS GHG Estimation Efficiency Emission
Pollutants Pollutants Method Code (Net after Factor
(T oos/Y ear) (Sec lnsttuctions) all controls)
2020
Criteria Emissions-Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission
Pollutants Code Pollutants Method Code (Net after Factor
(Tons/Yeat) (Sec Instructions) all controls)
2020 co co 08
NOx NOx 08
TSP TSP 08
PMJO PMl0 08
PM2.5 PM2.5 08
SO2 SO2 08 voe voe 0.01 10 0.0028
Emissions Emission Control HAP/TAP CAS Estimation Emission
Pollutants (In Alphabetical Order} (sec instructions) HAP/TAPS Method Code Efficiency Factor (l'ounds/Y car) (Net after all controls)
(See lnsttuctions)
2020
24%
Ef
Control
Ef
Control
EF
Control
31
Operating Scenario: OS -70 Emission Source/Group ID: CP-001
10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2020)
Hours per Day ( 22 ) Days per Week ( 7 ) Weeks per Year ( 50 )
11. Typical Start & End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throughput:
Jan-Feb + Dec
2020 25% March-May
2020 24% June-Aug.
2020 27% Sept.-Nov.
2020
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions-Emission Control GHG CAS GHG Estimation Efficiency Emission
Pollutants Pollutants Method Code {Net after Factor
(Tons/Year) (See Instructions) all conuols)
2020
Criteria Emissions-Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission
Pollutants Code Pollutants Method Code (Net after Factor
(Tons/Year) (Sec Instructions) all controls)
2020 co co 08 0
NOx NOx 08 0
TSP TSP 4.4 10 98 1.18
PM10 PM10 4.4 10 98 1.1 8
PM2.5 PM2.5 4.4 10 98 1.18
SO2 SO2 08 0 voe voe 9.1 10 0 2.44
Emissions Emission Control HAP/TAP CAS Estimation Emission
Pollutants (In Alphabetical Order) (sec instructions) HAP/TAPS Method Code Efficiency Factor (Pounds/Y car)
(See Instructions)
(Net after all controls)
2020
24%
Ef
Control
Ef
Control
AFTER
AFTER
AFTER
AFTER
EF
Control
33
Operating Scenario: OS - 2
Emission Source/Group ID: CP-002
10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2020)
Hours per Day ( 22 ) Days per Week ( 7 ) Weeks per Year ( 50 )
11. Typical Start & End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throughput:
25% March-May
2020 24% J une-Aug.
2020 27% Sept.-Nov.
2020
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions-Emission Control GHG CAS GHG Estimation Efficiency Emission
Pollutants PoJlutants Method Code (Net after Factor
(Ton.vY car) (Sec lnStructions) all controls)
2020
Criteria Emissions-E mission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission
Pollutants Code Pollutants Method Code (Net after Factor
(Tons/Year) (See Instructions) all controls}
2020 co co 08 0
NOx NOx 08 0
TSP TSP 2.16 10 98 0.58
PMIO PMlO 2.16 10 98 0.58
PM2.5 PM2.5 2.16 10 98 0.58
SO2 SO2 08 0
voe voe 51.07 10 0 13.7
Emissions Emission Control HAPffAP CAS Estimation Emission
Pollutants (ln Alphabetical Order) (sec instructions) HAPffAPS Method Code Efficiency Factor (Pounds/Year) (Nel after all controls)
(See lostructions)
2020
Formaldehyde 50-00-0 3166.4 08 0
Methanol 67-56-1 51 071.6 08 0
Methylene dipbenyl
diisocyanate (MDI) 101-68-8 20.87 08 0
(Component of POMTV)
Phenol 108-95-2 590.45 08 0
24%
Ef
Control
Ef
Control
AFTER
AFTER
AFTER
AFTER
EF
Control
AFTER
AFTER
AFTER
AFTER
35
Operating Scenario: OS -59 Emission Source/Group ID: CP-006
10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2020)
Hours per Day ( 21 ) Days per Week ( 6 ) Weeks per Year ( 50 )
11. Typical Start & End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throughput:
Jan-Feb + Dec
2020 25% March-May
2020 24% June-Aug.
2020 27% Sept.-Nov.
2020
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions-Emission Control GHG CAS GHG Estimation Efficiency Emission
Pollutants Pollutants Method Code (Net after Factor
(Tons/Year) (Sec Instructions) all controls)
2020
Criteria Emissions-Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission
Pollutants Code Pollutants Method Code (Nc1 after Factor
(Tons/Year) (Sec Instructions) all controls}
2020
co co 08 0
NOx NOx 08 0
TSP TSP 3.27 10 98 1.06
PMlO PMlO 3.27 10 98 1.06
PM2.5 PM2.5 3.27 10 98 1.06
SO2 SO2 08 0
voe voe 5.03 10 0 1.63
Emissions E mission Control HAP/TAP CAS Estimation Emission
Pollutants (In Alphabetical Order) (sec instructions) HAP/TAPS Method Code Efficiency Factor {Pounds/Year) (Net aflcr all controls)
(See Instructions)
2020
24%
Ef
Control
Ef
Control
AFTER
AFTER
AFTER
AFTER
EF
Control
37
Operating Scenario: OS -7 Emission Source/Group ID: CP-007
10. Operating Schedule:(Source/0peratingScenario that best characterizes Calendar Year 2020)
Hours per Day ( 22 ) Days per W eek ( 6 ) Weeks per Year ( 50 )
11. Typical Start & End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throughput:
Jan-Feb + Dec
2020 25% March-May
2020 24% June-Aug.
2020 27% Sept.-Nov.
2020
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions-Emission Control GHG CAS GHG Estimation Efficiency Emission
Pollutants Pollutants Method Code (Net after Factor
(Tons/Year) (Sec lo.struction.s) all controls)
2020
Criteria E missions-Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission
Pollutants Code Pollutants Method Code {Net aficr Factor
(Tons/Year) (See ln.struc1ions) all controls)
2020
co co 08 0
NOx NOx 08 0
TSP TSP 0.06 10 98 0.02
PMlO PMlO 0.06 10 98 0.02
PM2.S PM2.5 0.06 10 98 0.02
SO2 SO2 08 0
voe voe 0.56 10 0 0.18
Emissions Emission Control HAP/TAP CAS Estimation Emission
Pollutants (In Alphabetical Order) (sec instructions) HAP/TAPS Method Code Efficiency Factor (Pounds/Year)
(See I n.structions)
(Net aficr all controls)
2020
Methanol 67-56-1 279.59 02 0
24%
Ef
Control
Ef
Control
AFTER
AFTER
AFTER
AFTER
EF
Control
AFTER
39
Operating Scenario: OS -20 Emission Source/Group ID: ENGl
10. Operating Scbedule:(Source/OperatingScenario that best characterizes Calendar Year 2020)
Hours per Day ( 1 ) Days per W eek ( 1 ) Weeks per Year ( 20 )
11. Typical Start & End Times For Operating Scenario: Start: 1200 End: 1400
12. Seasonal Periods Percent Annual Throughput:
Jan-Feb + Dec
2020 19% 29% June-Aug.
2020 19% Sept.-Nov.
2020
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions-E mission Control GHG CAS GHG Estimation Efficiency Emission
PoUutants Pollutants Method Code (Net after Factor
(Ton;S/Ycar) (Sec l0s1ructions) all controls)
2020
Criteria Emissions-E mission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission
Pollutants Code Pollutants Method Code (Net after Factor
(Tons/Year) (See lnslructions) all controls)
2020
co co 0.04 08 7.3
NOx NOx 0.18 08 32
TSP TSP 0.01 08 0.93
PMlO PMlO 0.01 08 0.93
PM2.5 PM2.5 0.01 08 0.93
SO2 SO2 0.03 08 5.4
voe voe 0.01 08 0.94
Emissions E mission Control HAP/TAP CAS Estimation Emission
Pollutants (In Alphabetical Order) (sec inslructions) HAP/TAPS Method Code Efficiency Factor (Pounds/Year) (Nel after all controls)
(Sec lnstIUctions)
2020
Acetaldehyde 75-07-0 0.00266 09 0.00024
Benzene 71-43-2 0.08103 09 0.0073
Formaldehyde 50-00-0 0.0082 1 09 0.00074
Naphthalene (Component 91-20-3 0.01332 09 0.0012 of POMTV)
Polycyclic Organic Matter
(Inc P AH, ,dioxins, etc. NC POM 0.0222 09 0.002 & AP 42 historic
amorphous glob)
Propylene oxide 75-56-9 0.2886 09 0.026
Toluene 108-88-3 0.02886 09 0.0026
Xylene 1330-20-7 0.01998 09 0.0018
33%
Ef
Control
Ef
Control
EF
Control
41
Operating Scenario: OS -21 Emission Source/G roup ID: F-1
10. Operating Scbedule:(Source/OperatingScenario that best characterizes Calendar Year 2020)
Hours per Day ( 23 ) Days per Week ( 7 ) Weeks per Year ( 49 )
11. Typical Start & End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throughput:
Jan-Feb + Dec
2020 25% March-May
2020 24% June-Aug.
2020 27% Sept.-Nov.
2020
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions- Emission Control GHG CAS GHG Estimation Efficiency Emission
Pollutants Pollutants Method Code (Net after Factor
(Tons/Year) (Sec Instructions) all controls)
2020
Criteria Emissions-E mission Control
(NAAQS) Pollutant Criter ia Estimation Efficiency Emission
Pollutants Code Pollutants Method Code (Net after Factor
(Tons/Year) (Sec lnsllllctions) all controls)
2020 co co 08
NOx NOx 08
TSP TSP 2.23 08
PMlO PMl 0 0.78 08
PM2.S PM2.5 0.78 08
SO2 SO2 08 voe voe 08
Emissions E mission Control HAPffAP CAS Estimation E mission
Pollutants (In Alphabetical Order) (see instructions) HAPffAPS Method Code Efficiency Factor (Pounds/Year) (Net a0cr all controls)
(See lns1ruetions)
2020
24%
Ef
Control
Ef
Control
EF
Control
43
Operating Scenario: OS -60 Emission Source/Group ID:
FUELPREP
10. Operating Schedule:(Source/0peratingSccnario that best characterizes Calendar Year 2020)
Hours per Day ( 17 ) Days per Week ( 7 ) Weeks per Year ( SO )
11. Typical Start & End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throughput:
Jan-Feb + Dec
2020 25% March-ay
2020 24% June-Aug.
2020 27% Sept.-Nov.
2020
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions-Emission Control GHG CAS GHG Estimation Efficiency Emission
Pollutants Pollutants Method Code (Net after Factor
(Tons/Year) (Sec Instructions) all controls)
2020
Criteria Emissions-E mission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission
Pollutants Code Pollutants Method Code (Net ofter Factor
(Tons/Year) (See Instructions) all controls)
2020 co co 08 0
NOx NOx 08 0
TSP TSP 1.77 10 98 0.66
PMl0 PMl0 1.77 10 98 0.66
PM2.5 PM2.5 1.77 10 98 0.66
SO2 SO2 08 0 voe voe 12.68 IO 0 4.73
Emissions Emission Control HAPffAP CAS Estimation Emission
Pollutants (In Alphabct,cal Order) (sec instructions) HAPffAPS Method Code Efficiency Factor (Pounds/Y car) (Net after all controls)
(See Instructions)
2020
Formaldehyde 50-00-0 57.12 04 0
Methanol 67-56-1 279.59 02 0
24%
Ef
Control
Ef
Control
AFTER
AFTER
AFTER
AFTER
EF
Control
AFTER
AFTER
45
Operating Scenario: OS -33 Emission Source/Group ID: IS-DF-1
10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2020)
Hours per Day ( t ) Days per Week ( 1 ) Weeks per Year ( 26 )
11. Typical Start & End Times For Operating Scenario: Start: 1200 End: 1230
12. Seasonal Periods Percent Annual Throughput:
Jan-Feb + Dec
2020 25% March-May
2020 25% J une-Aug.
2020 25% ept.-Nov.
2020
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions-Emission Contr ol GHG CAS GHG Estimation Efficiency Emission
Pollutants Pollutants Method Code (Net after Factor
(Toas/Y car) (Sec Instructions) all controls)
2020
Criteria Emissions-Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission
Pollutants Code Pollutants Method Code (Net after Factor
(Tons/Y car) (Sec Instructions) all controls)
2020 co co 0.02 09 1.837
NOx NOx 0.09 09 8.525
TSP TSP 0.01 08 0.605
PMl0 PMl0 0.01 08 0.605
PM2.5 PM2.5 0.01 08 0.605
SO2 SO2 0 08 0.3337 voe voe 0.01 09 0.6914
Emissions Emission Control HAP/TAP CAS Estimation Emission
Pollutants (In Alphabetical Order) (sec instructions) HAP/TAPS Method Code Efficiency Factor (Pounds/Y car) (Net after all controls)
(Sec Instructions)
2020
Acetaldehyde 75-07-0 0.03218 09 0.001476
Acrolein 107-02-8 0.00388 09 0.0001781
Arsenic Unlisted
Compounds ( Specify & ASC-Other 0.00017 09 0.0000077
Component of ASC)
Benzene 71-43-2 0.03915 09 0.001796
Beryllium metal
(unreacted) (Component 7440-41-7 0.00013 09 0.0000058
ofBEC)
Cadmium Metal
(elemental unreacted, 7440-43-9 0.00013 09 0.0000058
Component of CDC)
Formaldehyde 50-00-0 0.04952 09 0.0022715
Lead Unlisted Compounds
(Specify and Component PBC-Other 0.00037 09 0.000017
of PBC)
25%
Ef
Control
Ef
Control
EF
Control
47
COPY of RECORD Date Submitte$!,11nQ/~l 11:27:35
NC Dept of'£n\11f
As entered in i&RCJ 2.0'l\
Facility Name: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Facility ID : 7300061
n .. 1 • gh Regional Office Permit : 077 60
~el County : Person Roxboro, NC 27574
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
1. Emission Source ID (from permit)
or Emission Source Group ID
2. Emission Source Description :
3. Operating Scenario ID/
Description:
IS-EO-1
Edgeseal operation consisting of 2 paint booths: one on the main line,
which also applies/sprays a logo and end strips; one on the T &G. End
strips are also applied to the product by water based aer
OS -77/Application of edgeseal to the finished product.
4. SCC Number/Description: 49099998/Miscellaneous Volatile Organic Compound Evaporation; Identify
the Process and Solvent in Comments
5. Throughput/units in 2020:
(e.g. production or fuel use):
6. Fuel Information
(If fuel is used)
7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
8. Control Device Information :None
Order CS-ID CD ID
186300 GAL/yr
(as listed in permit)
I Heat Content I
(Brulooiu)
Control Device Description
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
(in feet) Circle (enter If): (F) (Feet/sec) Rate (Acfm) Rectangle (L x W)
(inO.I feet)
ERP FUGITIVE (NO 1 72 Area = I edgeseal STACK)
ERP Description
Edgeseal booth
does not vent
outside
49
COPY of RECORD Date Submitted: 6/30/202111:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Roxboro, NC 27574
North Carolina Department of Environmental Quality
Division of Air Quality
Facility ID : 7300061
Permit: 07760
County : Person
DAQ Region : RRO
Air PolJutant Point Source Emissions Inventory-Calendar Year 2020
1. Emission Source ID (from permit)
or Emission Source Group ID
2. Emission Source Description :
3. Operating Scenario ID/
Description:
IS-PO-I
Printing operations consisting of the Logo and AP A stamp operations
and Re-grade. The AP A stamp goes on the saw line, where the Logo
goes on in the paint booth. Boards that fail quality standards re
OS -78/Stamp ink
4. SCC Number/Description: 49099998/Miscellaneous Volatile Organic Compound Evaporation; Identify
the Process and Solvent in Comments
5. Throughput/units in 2020:
(e.g. production or fuel use):
6. Fuel Information
(If fuel is used)
7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
8. Control Device Information :None
Order CS-ID CDID
3375 GAL/yr
%Sulfur
(as listed in permit)
%Ash Heat Content
(Btu/units)
Control Device Description
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
{in feet} Cirdc {enter#}: (F) (Feet/sec) Rate (Adm) Rectangle (L x W}
(in 0.1 feet}
erp-fug FUGITIVE (NO I 72 Area = I STACK)
ERP Description
ERP for Fugitive
sources
51
COPY of RECORD Date Submitted: 6/30/202111:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
I 04 75 Boston Road
Roxboro, NC 27574
North Carolina Department of Environmental Quality
Division of Air Quality
Facility ID : 7300061
Permit: 07760
County : Person
DAQ Region : RRO
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
1. Emission Source ID (from permit)
or Emission Source Group ID
2. Emission Source Description :
3. Operating Scenario ID/
Description:
4. SCC Number/Descr iption:
5. Throughput/units in 2020:
(e.g. production or fuel use):
6. Fuel Information
(If fuel is used)
7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
8. Control Device Information :None
Order CS-W CDID
IS-WE-I
volatile organic liquid storage tank (12,000 gallon capacity)
OS -67/Extra Operating Scenario -Delete
40799999/Miscellaneous; Other Not Classified
¾Sulfur ¾Ash Heat Content
(Btu/units)
Control Device Description
(as listed in permit)
9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle (enter#): (F) (Feet/sec) Rate (Acfm) Rectangle (L x W)
(in 0.1 feet)
erp-fug FUGITIVE (NO I 72 Area = 1 ERP for Fugitive
STACK) sources
53
COPY of RECORD Date Submitted: 6/30/202111:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Roxboro, NC 27574
Facility ID : 7300061
Permit : 07760
County : Person
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
1. Emission Source ID (from permit)
or Emission Source Group ID
2. Emission Source Description :
3. Operating Scenario ID/
Description:
4. SCC Number/Description:
5. Throughput/units in 2020:
(e.g. production or fuel use):
6. Fuel Information
(If fuel is used)
7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
8. Control Device Information :None
Order CS-ID CDID
IS-WE-I
volatile organic liquid storage tank (12,000 gallon capacity)
OS -68/wax storage
40799999/Miscellaneous ; Other Not Classified
2986076 LB/yr
%Sulfur %Ash Heat Content
(Btu/units)
Control Device Description
(as listed in permit)
9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):
ERPID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Cin:le (enter#): (F) (Feet/sec) Rate (Aerni) Rectangle (L x \V)
(in 0.1 feet)
erp-fug FUGITIVE (NO 1 72 Area= l ERP for Fugitive
STACK) sources
55
Facility Total CY 2020 Emissions Summary
COPY of RECORD Date Submitted: 6/30/202111:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Roxboro, NC 27574
North Carolina Department of Environmental Quality
Division of Air Quality
Facility ID : 7300061
Permit: 07760
County : Person
DAQ Region : RRO
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
Record Facility-Wide Totals From all Permitted and on-Permitted AirPollutant Emission Sources
Green House Gases Pollutants GHG
Actual Emissions (Tons/Year)
Pollutant CAS 2020 2019 % C hange
Criteria Pollutants
Actual Emissions (Tons/Year)
Pollutant CAS 2020 2019 % Change
co co 116.33 101.77 14.306775%
NOx NOx 141.26 135.49 4.258609%
PM(TSP) TSP 68.1 66.3 2.714925%
PMlO PMlO 66.38 64.6 2.7554162%
PM2.5 PM2.5 66.38 64.6 2.7554162%
S02 S02 6.84 8.81 -22.360956%
voe voe 129.9 127.85 1.603438%
Hazardous Air PolJutants<HAPS) and/or Toxic Air PolJutants(TAPs)
I I Actual Emissions (Pounds/Year) I
Pollutant ICAS 12020 12019 1% Change
Pollutant Group:Antimony & Compounds (total mass, inc elemental SB) Group Sum: 1.8246
Antimony Unlisted Compounds I SBC-Other 11.8246 12.1364 1-14.5946455% (Specify & Component of SBC)
Pollutant Group:Arsenic & Compounds (total mass of elemental AS, arsine and all inorganic compounds) Group Sum:4.70017
Arsenic Unlisted Compounds ( IASC-Other 14.70017 14.66027 I 0.8561698% Specify & Component of ASC)
Pollutant Group:Beryllium & compounds (Total mass) Group Sum:.25423
Beryllium metal (unreacted) 17440-41-7 10.25423 1.29771 1-14.60482% (Component of BEC)
Pollutant Group:Cadmium & compounds (total mass inc elemental metal) Group Sum:1.18473
Cadmium Metal (elemental 17440-43-9 11.18473 11.32661 1-10.694923% unreacted, Component of CDC)
Pollutant Group:Chromium (VI) Soluble Chromate Compounds (Component of CRC) Group Sum:.9434
Chromic acid (VI) (Component of 17738_94_5 SolCR6 & CRC) 10,9434 11.0505 1-10. 195146%
Pollutant Group:Chromium -Allffotal (Inc Chromium {VI) categories, metal and Others) Group Sum: 14.8054
57
Methyl isobutyl ketone 108-10-1 788.61 776.55 1.5530227%
Methylene chloride 75-09-2 217.347 221.168 -1.7276455%
Nitrophenol, 4-100-02-7 0.0127 .0149 -14.7651005%
Pentachlorophenol 87-86-5 0.0059 .0066 -10.606057%
Perchloroethylene 127-18-4 4.3883 5.14 -14.624512% ( tetrachloroethylene)
Phenol 108-95-2 7946.241 7858.2 1.1203712%
Polychlorinated biphenyls (PCB) 1336-36-3 0.0014 .0016 -12.500001%
Polycyclic Organic Matter (Inc
PAH, dioxins, etc. NC & AP 42 POM 0.60265 .66604 -9.517448%
historic amorphous glob)
Propionaldebyde 123-38-6 5969.65 5904.77 1.0987707%
Propylene dichloride 78-87-5 3.8109 4.4621 -14.594026%
Propylene oitide 75-56-9 0.2886 .255 13.176472%
Selenium Compounds SEC 0.65063 .76103 -14.506658%
Styrene 100-42-5 444.1329 479.3015 -7.3374705%
Toluene 108-88-3 743.94904 738.86181 0.6885211%
Trichlorobenzene, 1,2,4-120-82-1 0.0371 .0434 -14.516134%
Trichloroethylene 79-01-6 3.4644 4.0565 -14.596325%
Trichlorophenol, 2,4,6-88-06-2 0.0025 .003 -16.66667%
Vinyl acetate 108-05-4 1378.402 I 135.9053 1 21.34832%
Vinyl chloride 75-01-4 2.0786 2.4339 -14.597977%
Xylene 1330-20-7 581.2772 570.55249 1.8797098%
59
Notes
1. No PF resin was used in 2020. All products 100% MDI.
2. Chromium acid (VI) increased his was primarily due to increased wood fuel
consumption in the bark burner and an update to the EF for gas in the TO H's.
LP Roxboro Facility ID: 7300061 Permit 07760T23
Oper ating Scenario: OS -60 Emission Source/G roup ID:
FUELPREP
10. Operating Schedule:(Source/0peratingScenario that best characterizes Calendar Year 2020)
Hours per Day ( 17 ) Days per Week ( 7 ) Weeks per Year ( 50 )
11. Typical Start & End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throughput:
J an-Feb + Dec
2020 25% March-May
2020 24% June-Aug.
2020 27% Sept.-Nov.
2020
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 E fficiency E m ission
Polluta nts Polluta nts Method Code (Net after F actor
(Tons/Year) (Sec Instructions) all controls)
2020
Criteria Emissions-Emission Control
(NAAQS) Pollu tant Criteria Estimation E fficiency E m ission
Pollutants Code Pollutants Method Code (Net after Factor
(Tons/Year) (See lnsttuctions) all controls)
2020
co co 08 0
NOx NOx 08 0
TSP TSP 1.77 10 98 0.66
PMl0 PMl 0 1.77 10 98 0.66
PM2.5 PM2.5 1.77 10 98 0.66
SO2 SO2 08 0
voe voe 12.68 10 0 4.73
Emissions Emission Control HAP/TAP CAS Estimation Emission
Pollutants (In Alphabetical Order) (see instructions) HAPffAPS Method Code E fficiency Factor (PoWlds/Y car) (Net after all controls)
(See Insttuctions)
2020
For maldehyde 50-00-0 57.12 04 0
Methanol 67-56-1 279.59 02 0
24%
Ef
Control
Ef
Control
AFTER
AFTER
AFTER
AFTER
EF
Control
AFTER
AFTER
45
Operating Scenario: OS -33 Emission Source/Group ID: IS-DF-1
10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2020)
Hours per Day ( 1 ) D ays per Week ( 1 ) Weeks per Year ( 26 )
11. Typical Start & End Times For Operating Scenario: Start: 1200 End: 1230
12. Seasonal Periods Percent Annual Th roughput:
Jan-Feb + Dec
2020 25% March-May
2020 25% June-Aug.
2020 25% Sept.-Nov.
2020
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions-Emission Control GHG CAS GHG Estimation Efficiency Emission
Pollutants Pollutants Method Code (Net after Factor
(Tons/Year) (Sec 1.nstructions) all controls)
2020
Criteria Emissions-Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission
Pollutants Code Pollutants Method Code (Net after Factor
(T ons/Y car) (Sec Instructions) all controls)
2020 co co 0.02 09 1.837
NOx NOx 0.09 09 8.525
TSP TSP 0.01 08 0.605
PMlO PMlO 0.01 08 0.605
PM2.5 PM2.5 0.01 08 0.605
SO2 SO2 0 08 0.3337 voe voe 0.01 09 0.6914
Emissions Emission Control HAPffAP CAS Estimation Emission
Pollutants (In Alphabetical Order) (sec instructions) HAP/TAPS Method Code Efficiency Factor (Pounds/Year) (Net after all controls)
(See Instructions)
2020
Acetaldehyde 75-07-0 0.03218 09 0.001476
Acrolein 107-02-8 0.00388 09 0.0001781
Arsenic Unlisted
Compounds ( Specify & ASC-Other 0.00017 09 0.0000077
Component of ASC)
Benzene 71-43-2 0.03915 09 0.001796
Beryllium metal
(unreacted) (Component 7440-41-7 0.00013 09 0.0000058
ofBEC)
Cadmium Metal
(elemental unreacted, 7440-43-9 0.00013 09 0.0000058
Component of CDC)
Formaldehyde 50-00-0 0.04952 09 0.0022715
Lead Unlisted Compounds
(Specify and Component PBC-Other 0.00037 09 0.000017
of PBC)
25%
Ef
Control
Ef
Control
EF
Control
47
COPY of RECORD Date Submitted: 6/30/202111:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Facility ID : 7300061
Permit: 07760
County : Person Roxboro, NC 27574
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
1. Emission Source ID (from permit)
or Emission Source Group ID
2. Emission Source Description :
3. Operating Scenario ID/
Description:
IS-EO-1
Edgeseal operation consisting of 2 paint booths: one on the main line,
w hich also applies/sprays a logo and end strips; one on the T &G. End
strips are also applied to the product by water based aer
OS -77/Application of edgeseal to the finished product.
4. SCC Number/Description: 49099998/Miscellaneous Volatile Organic Compound Evaporation ; Identify
the Process and Solvent in Comments
5. Throughput/units in 2020:
(e.g. production or fuel use):
6. Fuel Information
(If fuel is used)
7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
8. Control Device Information :None
Order CS-ID CDID
186300 GAL/yr
(as listed in permit)
I "~· Co'.""' I
(Btu/uruts)
Control Device Description
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
(in feet) Circle (enter#): (F) (Feet/sec) Rate (Acfm) Rectangle (L x W)
(in 0. I feet)
ERP FUGITIVE (NO 1 72 Area= 1 edgeseal STACK)
ERP Description
Edgeseal booth
does not vent
outside
49
COPY of RECORD Date Submitted: 6/30/2021 11:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
104 7 5 Boston Road
Roxboro, NC 27574
North Carolina Department of Environmental Quality
Division of Air Quality
Facility ID : 7300061
Permit : 07760
County : Person
DAQ Region : RRO
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
1. Emission Source ID (from permit)
or Emission Source Group ID
2. Emission Source Description :
3. Operating Scenario ID/
Description:
IS-PO-1
Printing operations consisting of the Logo and AP A stamp operations
and Re-grade. The AP A stamp goes on the saw line, where the Logo
goes on in the paint booth. Boards that fail quality standards re
OS -78/Stamp ink
4. SCC Number/Description: 49099998/Miscellaneous Volatile Organic Compound Evaporation ; Identify
the Process and Solvent in Comments
S. Throughput/units in 2020:
(e.g. production or fuel use):
6. Fuel Information
(If fuel is used)
7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
8. Control Device Information :None
Order CS-ID CD ID
3375 GAL/yr
(as listed in permit)
I H~, eo,ren, I
(Btu/units)
Control Device Description
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
(in feet) Circle (toter#): (F) (Feet/sec) Rate (Acfm) Rectangle (L X W)
(in 0.1 feet)
erp-fug FUGITIVE (NO 1 72 Area = 1 STACK)
ERP Description
ERP for Fugitive
sources
51
Phenol-Formaldehyde Tank Emissions
Basis: Number of Tanks
Actual Throughput
Maximum Annual Throughput
Tank Size
Tank Diameter
Tank Height
Tank Shell Height
Tank Liquid Height
Fill Rate
Maximum Fill Rate
Material Classification (Crude Oil or VOC)
Specific Gravity of Resin
Vapor Pressure of Resin at 25 deg C
Conversion Factor (Gallons per Barrel)
Conversion Factor (psia per aim)
Conversion Factor (mmHg per aim)
Henry's Constants
Formaldehyde
Phenol
Weight Percentage of Resin Constituents
Formaldehyde
Phenol
Molecular Weights
Formaldehyde Mv
Phenol Mv
2 tanks
0.0 gallons/yr
/ltiNIIN/fllfl gallons/yr
15000 gallons
12 ft
18 ft
16 ft
16 ft
30000 gal/hr
30000 gal/hr
voe
1.3
22 mmHg
0.43 psia
42 gallons/bbl
14.7 psi/atm
760 mmHg/atm
3.40E-07 aim m3/g mol
1.30E-06 aim m3/g mol
1 %
1 %
30 lbllb-mol
94 lb/lb-mol
Partial Pressures-Calculation Methodology from Strohbeck fax dated 1/14/97
Formaldehyde PvA
[(0.00000034 aim m3/g mol) • (14.7 psi/aim)• (0.01 ) • (1.3) • (1000000 g /m3)) / (30
0.00217 psia
Phenol PvA
1(0.0000013 aim m3/g mol) • (14.7 psi/aim)• (0.01) • (1.3) • (1000000 g /m3)] / (94 g
0.00264 psia
O actualhou,ty
30000 gal/hr/ 42 gallons/bbl = 714 bbl/hr
O actuai annual
0 gallons/yr I 42 gallons/bbl = 0 bbl/yr
Nactua1
5.614 • 0 bbl/yr/ (2 tanks• pi• 11.58 flh2 • 15.75 ft)=
0
LP Roxboro Facility ID: 7300061
Permit No. 07760T24
COPY of RECORD Date Submitted: 6/30/202111:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Roxboro, NC 27574
North Carolina Department of Environmental Quality
Division of Air Quality
Facility ID : 7300061
Permit : 07760
County : Person
DAQ Region : RRO
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
1. Emission Source ID (from permit)
or Emission Source Group ID
2. Emission Source Description :
3. Operating Scenario ID/
Description:
4. SCC Number/Description:
5. Throughput/units in 2020:
(e.g. production or fuel use):
6. Fuel Information
(If fuel is used)
7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
8. Control Device Information :None
Order CS-ID LIJID
IS-WE-1
volatile organic liquid storage tank (12,000 gallon capacity)
OS -67/Extra Operating Scenario -Delete
40799999/Miscellaneous ; Other Not Classified
I Hut Con~nt I
(Btu/units)
Control Device Description
(as listed in permit)
9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):
ERPID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle (enter If): (F) (Feet/see) Rate (Adm) Rectangle (L x W)
(in 0.1 feet)
erp-fug FUGITIVE (NO 1 72 Area= 1 ERP for Fugitive
STACK) sources
53
COPY of RECORD Date Submitted: 6/3 0/202111:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Roxboro, NC 27574
Facility ID: 7300061
Permit : 07760
County : Person
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
1. Emission Source ID (from permit)
or Emission Source Group ID
2. Emission Source Description :
3. Operating Scenario ID/
Description:
4. SCC Number/Description:
5. Throughput/units in 2020:
(e.g. production or fuel use):
6. Fuel Information
(If fuel is used)
7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
8. Control Device Information :None
Order CS-ID l.:V ID
IS-WE-1
volatile organic liquid storage tank (12,000 gallon capacity)
OS -68/wax. storage
40799999/Miscellaneous ; Other Not Classified
2986076 LB/yr
I Hoot Coarent I
(Btu/units)
Control Device Description
( as listed in permit)
9. Emission R elease Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):
ERPID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feel) Circle (enter#): (F) (Feel/sec) Rate (Adm) Rectangle (L X W)
(in 0.1 feet)
erp-fug FUGITIVE (NO 1 72 Area = 1 ERP for Fugitive
STACK) sources
55
Phenol-Fonnaldehyde Tank Emissions
Equation:
Emissions are based on AP-42, 5th Edition Chapter 7. These tanks are located in a
controlled environment. Therefore, the temperature of these tanks does not vary. A
the tanks do not have any breathing loss. The storage tank emission calculation pro
then simplifies to the equation below.
Lw = 0.0010 • Mv • PvA • Q •KN• Kp
Lw
Mv
PvA
Q
~
Kp
N
where:
where:
HLX
D
therefore:
LP Roxboro
Working Loss, lbs/yr
Vapor Molecular Weight, lb/lb-mol
Partial Pressure at Daily Average Liquid Surface Temperature, psii
Annual Net Throughput, bbVyr
Turnover Factor, dimensionless, (180 + N)/6N for N >36 else 1
Working Loss Product Factor Is 1 Unless a Crude Oil Then 0.75
Number of Turnovers
N = 5.614QNLX
Tank Maximum Liquid Volume, cu. ft
vl.X = pi • o i14 • Hl.X
Maximum Liquid Height, ft
Tank Diameter, ft
N = 5.614 •QI (pi* 02/4 • H)
Facility ID: 7300061
Permit No. 07760T24
Notes
1. No PF resin was used in 2020. All products 100% MDI.
2. Chromium acid (VI) increased his was primarily due to increased wood fuel
consumption in the bark burner and an update to the EF for gas in the TOH's.
LP Roxboro Facility ID: 7300061 Permit 07760T23
Stack Data
Stack Data:
last control Stack Height Height Diameter Stack area
meters feet feet s .ft.
cyclone CP-001 13.7 45.0 4.8 17.7
baghouse CP-002 24.7 81.0 1.8 2.6
cyclone CP-003 8.5 28.0 3.8 11.5
cyclone CP-005 13.1 43.1 4.8 17.7
cyclone CP-006 7.6 25.0 3.8 11.5
baghouse CP-007 18.9 62.0 0.8 0.5
cyclone CP-008 19.5 64.0 3.3 8.7
RTO RTO-3 80.0 6.9 37.4
DryerRTOs RTO's4-6 33.5 110.0 9.0 63.6
Data Modeling Modeling Modeling Calculated
•Note: For RTO Stack Testin
Modeling Report:
Louisiana-Pacific Corporation, Roxboro Oriented Strandboard
Roxboro, Person County, North Carolina
Stack Testing Report:
LP Roxboro
Facility ID: 7300061
Page 21
Velocity Velocity Flow Rate Exit Temp
mis f/s) wet acfm F
9.0 93.6 31 ,360.0 75
27.8 91.3 14,460.0 75
5.9 19.4 13,440.0 75
9.6 31.5 33,400.0 75
11.6 37.9 26,240.0 75
4.5 14.7 480.0 75
8.7 28.6 15,000.0 75
61.2 137,201.0 261
76.2 290,686.0 245
Calculated Calculated Calculated* Modeling
Permit No. 07760T24
Phenol-Formaldehyde Tank Emissions
KN actual
Since N < or equal to 36 the value is
Kp
Materials other than crude oil have a value of
Emission Calculations:
Pollutant Actual Emissions
Name (lbs/hr) (lbslvrl (tons/vr)
voe 0.2232 0.00 0
Formaldehyde 0.046 0.00 0
Phenol 0.1772 0.00 0
Formaldehyde Actual Emissions (lbs/hr)
0.001 • 30 lb/lb-mol * 0.00217 psia • 714 bbVhr • 1 • 1 =
Formaldehyde Actual Emissions (lbs/yr)
0.001 * 30 lb/lb-mol • 0.00217 psia * 0 bbl/yr * 1 * 1 =
Formaldehyde Actual Emissions (tons/yr)
o lbs/yr/ 2000 lbs/ton =
Phenol Actual Emissions (lbs/hr)
0.001 * 94 lb/lb-mo1 • 0.00264 psia * 714 bbVhr * 1 * 1 =
Phenol Actual Emissions (lbs/yr)
0.001 * 94 lb/lb-mol * 0.00264 psia • 0 bbl/yr * 1 * 1 =
Phenol Actual Emissions (tons/yr)
0 lbs/yr / 2000 lbs/ton =
voe Actual Emissions (lbs/hr)
0.046 lbs/hr+ 0.1772 lbs/hr=
voe Actual Emissions (lbs/yr)
0 lbs/hr + 0 lbs/hr =
voe Actual Emissions (tons/yr)
0 lbs/yr/ 2000 lbs/ton =
0.046 lbs/hr
0 lbs/yr
o tons/yr
0.1772 lbs/hr
0 lbs/yr
0 tons/yr
0.2232 lbs/hr
0 lbs/yr
0 tons/yr
LP Roxboro Facility ID: 7300061
Permit No. 07760T24
CP-001 Finishing process -sawtrim and CS-12 bagfilter (5,235 square feet of filter area) B-1
finishing line clean-up operation
CP-002 OSB forming process - blender and CS-9 bagfilter (2,219 square feet of filter area) B-2
forming bin aspiration systems
CP-003 Fuel Prep System -raw fuel bin CS-6 bagfilter (2,219 square feet of filter area) B-3
transfer system
Fuel Prep System -raw fuel bin
CP-004 loading system (high pressure CS-6 bagfilter (2,219 square feet of filter area) B-3
blower)
CP-005 OSB forming process -mat reject and
flying saw system
Finishing process -tongue and
CP-006 groove and sanderdust aspiration CS-13 bagfilter (3,698 square feet of filter area) B-6
system
CP-007 Fuel Prep System -sanderdust bin
transfer and loading system CS-7 bagfilter (69 square feet of filter area) B-7
bypass cyclone (120 inches in -
CYC5 diameter)
Saw trim recovery (screen) cyclone
CYC9 (84 inches in diameter) exhausting to CS-6 bagfilter (2,219 square feet of filter area) B-3
CP-003
diesel-fired emergency generator
ENGl (1,332 horsepower) [MACT Subpart
ZZZZ]
F-1 bark handling fugitives
FUELPREP Fuel Prep System -metering bin CS-8 bagfilter (2,219 square feet of filter area) B-8 transfer and loading system
IS-B-1 battery charging operation
IS-BC-1 blade cleaning operation
IS-BS-1 bench scale grinding
paint spray booth (Group l
IS-C-1 miscellaneous coating operations)
[MACTDDDD]
IS-CO-1 compressor oil
IS-CT-I cutting torch
IS-D-1 diesel fuel tank
IS-DB-1 dedarker
IS-DD-la Zep cleaning station -degreaser drum
(55 gallons)
IS-DD-lb Zep cleaning station -degreaser drum
(55 gallons)
IS-DF-1 diesel fire pump (275 bhp) (MACT
ZZZZ]
Edgeseal operation consisting of2
paint booths:one on the main line,
which also applies/sprays a logo and
end strips;one on the T&G. End strips
IS-EO-1 are also applied to the product by
water based aerosol cans just next to
the spray booth. (Group 1
miscellaneous coating operations)
[MACTDDDD]
IS-G-1 gasoline fuel tank
IS-HH-1 hand held grinding equipment
IS-HO-1 hydraulic oil storage reservoir
IS-HO-2 hydraulic oil system
IS-HO-3 hydraulic oil tank (19,800 gallons)
IS-MDI-3 volatile organic liquid or soybean oil
storage tank (30,000 gallon capacity)
4
COPY of RECORD Date Submitted: 6/30/202111:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Roxboro, NC 27574
'
Facility ID : 7300061
Permit : 07760
County : Person
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
1. Emission Source ID (from permit) FUELPREP
or Emission Source Group ID -------------------------
2. Emission Source Description : metering bin loading transfer system with bypass cyclone
3. Operating Scenario ID/ OS -60/W ood fuel metering bin collection
Description:
4. SCC Number/Description: 30700803/Sawmill Operations ; Sawdust Pile Handling
5. Throughput/units in 2020:
(e.g. production or fuel use):
6. Fuel Information
(If fuel is used)
7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
8. Control Device Information :
Order CS-ID CDID
5362.1 HR/yr
100
(as listed in permit)
1 CS-8 B-8
I Ho,t Conrent I
(Btu/umts)
Control Device Description
One bagfilter (2,219 square feet of filter area)
9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle (enter #): (F) {Feet/sec) Rate (Acfm) Rectangle (L x W)
(in 0.1 feet)
CP008 VERTICAL 64 3.3 75 28.6 14676.92 circular stack for
STACK fuel prep
44
COPY of RECORD Date Submitted: 6/30/202111:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Roxboro, NC 27574
Facility ID : 7300061
Permit : 07760
County : Person
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
1. Emission Source ID (from permit) F-1
or Emission Source Group ID --------------------------
2. Emission Source Description : bark handling fugitives --------------------------
3. Operating Scenario ID/ OS -21/bark handling fugitives _______ ....;;;._~----------------Description:
4. SCC Number/Description: 30700822/Sawmill Operations ; Chip Transfer/Conveying
5. Throughput/units in 2020:
(e.g. production or fuel use):
6. Fuel Information
(If fuel is used)
7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
8. Control Device Information :None
Order CS-ID CDID
7830.87 HR/yr
(as listed in permit)
I Heat Contont I
(Btu/units)
Control Device Description
9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):
ERPID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle (enter#): (F) (Feet/sec) Rate (Adm) Rectangle (L x W)
(in 0.1 feet)
erp-fug FUGITIVE (NO 1 72 Area = l ERP for Fugitive
STACK) sources
42
COPY of RECORD Date Submitted: 6/30/202111:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Facility ID : 7300061
Permit: 07760
County : Person Roxboro, NC 27574 DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
1. Emission Source ID (from permit)
or Emission Source Group ID
2. Emission Source Description :
3. Operating Scenario ID/
Description:
4. sec Number/Description:
5. Throughput/units in 2020:
(e.g. production or fuel use):
6. Fuel Information
(If fuel is used)
7. Capture Efficiency
(% ofEmissions from this Process Vented
to Control Device or Stack):
8. Control Device Information :None
Order CS-ID CDID
ENGl
diesel-fired emergency generator (1,332 horsepower) [MACT Subpart
ZZZZ]
OS -20/diesel-fired emergency generator (1 ,332 horsepower)
20100102/Distillate Oil (Diesel) ; Reciprocating
11.1 HR/yr
1 H~, eon,~, I
(Btu/units)
Control Device Description
(as listed in permit)
9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle (enter#): (F) (Feet/sec) Rate (Acfm) Rectangle (L x W)
(in 0.1 feet)
erp-fug FUGITIVE (NO 1 72 Area = 1 ERP for Fugitive
STACK) sources
40
COPY of RECORD Date Submitted: 6/30/202111:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
104 7 5 Boston Road
Roxboro, NC 27574
Facility ID : 7300061
Permit: 07760
County : Person
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
1. Emission Source ID (from permit) CP-007
or Emission Source Group ID -------------------------
2. Emission Source Description : Fuel Prep System -sanderdust bin transfer and loading system
3. Operating Scenario ID/ OS -7 /sanderdust bin transfer and loading system
Description:
4. SCC Number/Description: 30700803/Sawmill Operations ; Sawdust Pile Handling
5. Throughput/units in 2020:
(e.g. production or fuel use):
6. Fuel Information
(If fuel is used)
7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
8. Control Device Information :
Order CS-ID CDID
6167.4 HR/yr
100
(as listed in pennit)
1 CS-7 B-7
I Hoot Conrent I
(Btu/umts)
Control Device Description
One bag:filter (479 square feet of filter area)
9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):
ERP HJ 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. I feel)
CP007 VERTICAL 62 0.8 75 14.7 443.34 Sander Dust Bin
STACK Stack
38
COPY of RECORD Date Submitted: 6/30/202111:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
104 7 5 Boston Road
Roxboro, NC 27574
Facility ID : 7300061
Permit: 07760
County : Person
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
1. Emission Source ID (from permit) CP-006
or Emission Source Group ID -------------------------
2. Emission Source Description : tongue and groove and sanderdust aspiration system with bypass cyclone
3. Operating Scenario ID/ OS -59/Sander dust collection from tongue and groove process
Description:
4. SCC Number/Description: 30700803/Sawmill Operations ; Sawdust Pile Handling
5. Throughput/units in 2020:
(e.g. production or fuel use):
6. Fuel Information
(If fuel is used)
7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
8. Control Device Information :
Order CS-ID CDID
6167.5 HR/yr
100
(as listed in permit)
1 CS-13 B-6
I H~t Con«nt I
(Btu/umts)
Control Device Description
One bagfilter (3,698 square feet of filter area)
9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):
ERPID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle ( enter #): (F) (Feet/sec) Rate (Acfm) Rec13ngle (L X W)
(in 0.1 feet)
VERTICAL circular stack for
CP006 STACK 25 3.8 75 37.9 25789.77 tongue & groove
system
36
COPY of RECORD Date Submitted: 6/30/202111:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Roxboro, NC 27574
Facility ID: 7300061
Permit: 07760
County : Person
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
1. Emission Source ID (from permit) CP-002
or Emission Source Group ID -------------------------
2. Emission Source Description : OSB forming process -blender and forming bin aspiration systems
3. Operating Scenario ID/ OS -2/blender and forming bin aspiration systems
Description:
4. SCC Number/Description: 30700822/Sawmill Operations ; Chip Transfer/Conveying
5. Throughput/units in 2020:
(e.g. production or fuel use):
6. Fuel Information
(If fuel is used)
7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
8. Control Device Information :
Order CS-ID CDID
7455.2 HR/yr
100
(as listed in permit)
1 CS-9 B-2
I H,.t Content I
(Btu/units)
Control Device Description
One bagfilter (2,219 square feet of filter area)
9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):
ERPID 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)
circular stack for
CP002 VERTICAL 81 1.8 75 91.3 13939.81 forming
STACK bin/aspiration
system
34
COPY of RECORD Date Submitted: 6/30/202111:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Roxboro, NC 27574
Facility ID: 7300061
Permit: 07760
County : Person
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
1. Emission Source ID (from permit) CP-001
or Emission Source Group ID -------------------------
2. Emission Source Description : sawtrim and finishing line clean-up with bypass cyclone
3. Operating Scenario ID/ OS - 70/sawtrim and finishing line clean-up with bypass cyclone
Description:
4. SCC Number/Description: 30700803/Sawmill Operations ; Sawdust Pile Handling
5. Throughput/units in 2020:
(e.g. production or fuel use):
6. Fuel Information
(If fuel is used)
7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
8. Control Device Information :
Order CS-ID CDID
7455.2 HR/yr
100
(as listed in permit)
1 CS-12 B-1
I -•~nrent I
(Btu/units)
Control Device Description
One bagfilter (5,235 square feet of filter area)
9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):
ERPID 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)
VERTICAL circular stack for
CP00l STACK 45 4.8 75 29 31486.29 saw/finishing
operations
32
COPY of RECORD Date Submitted: 6/30/202111:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Facility ID : 7300061
Permit: 07760
County : Person Roxboro, NC 27574 DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
1. Emission Source ID (from permit)
or Emission Source Group ID
2. Emission Source Description :
3. Operating Scenario ID/
Description:
4. SCC Number/Description:
5. Throughput/units in 2020:
(e.g. production or fuel use):
6. Fuel Information
(If fuel is used)
7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
8. Control Device Information :None
Order CS-ID CDID
Group G-74 consisting ofIS-CO-1, IS-CT-1, IS-D-1, IS-DD-la, IS-G-1,
IS-HH-1, IS-HO-I, IS-HO-3, IS-PP-1, IS-TO-1, IS-UO-1, IS-B-1, IS-
BC-1, IS-BS-1, IS-C-1, IS-DB-1, IS-HO-2, IS-N-1 , IS-P-1, IS-SP-1, IS-
DD-lb, IS-W-2, IS-W-3, IS-WC-1
Miscellaneous Insignificant Activities with Minimal Emissions
OS -85/Nail line and Stencil
39999995/Miscellaneous Industrial Processes ; Other Not Classified
10125 GAL/yr
I Hut Conrent I
(Btu/umts)
Control Device Description
(as listed in permit)
9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):
ERPID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle (enter#): (F) (Feet/sec) Rate (Acfm) Rectangle (L X W)
(in 0.1 feet)
erp-fug FUGITIVE (NO 1 72 Area = 1 ERP for Fugitive
STACK) sources
30
Operating Scenario: OS -63 Emission Source/Group ID: G-67
10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2020)
Hours per Day ( 22 ) Days per Week ( 7 ) Weeks per Year ( 50 )
11. Typical Start & End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throughput:
Jan-Feb + Dec
2020 25% March-May
2020 24% June-Aug.
2020 27% Sept.-Nov.
2020
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions-Emission Control GHG CAS GHG Estimation Efficiency Emission
Pollutants Pollutants Method Code (Net after Factor
(Tons/Year) (See Instructions) all controls)
2020
Criteria Emissions-Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission
Pollutants Code Pollutants Method Code (Net after Factor
(Tons/Year) (See Instructions) all controls)
2020
co co 5.58 10 0
NOx NOx 6.82 10 0
TSP TSP 20.45 10 55
PMlO PM10 20.45 10 55
PM2.5 PM2.5 20.45 10 55
SO2 SO2 0.06 08 0
voe voe 4.65 10 98
Emissions Emission Control HAP/TAP CAS Estimation Emission
Pollutants (In Alphabetical Order) (see instructions) HAP/TAPS Method Code Efficiency Factor
(Pounds/Year) (Net after all controls)
(See Instructions)
2020
Acetaldehyde 75-07-0 1118.27 04 95
Acrolein 107-02-8 1192.82 04 95
Benzene 71-43-2 29.82 04 95
Benzo(a)pyrene
(Component of PO MTV & 50-32-8 0.00012 08 0
POM7)
Cadmium Metal
( elemental unreacted, 7440-43-9 0.1064 08 0
Component of CDC)
Chromic acid (VI)
(Component of SolCR6 & 7738-94-5 0.135 08 66
CRC)
Cumene 98-82-8 5107.16 08 95
Dichlorobenzene(p ), 1,4-106-46-7 0.1161 09 95
Formaldehyde 50-00-0 1301.06 04 74
Hexane, n-110-54-3 174.15 09 95
24%
Ef
Control
Ef
Control
AFTER
AFTER
AFTER
AFTER
AFTER
AFTER
EF
Control
AFTER
AFTER
AFTER
AFTER
AFTER
AFTER
AFTER
AFTER
AFTER
AFTER
28
Operating Scenario: OS -62 Emission Source/Group ID: G-63
10. Operating Schedule:(Source/0 peratingScenario that best characterizes Calendar Year 2020)
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 Throughput:
Jan-Feb+ Dec
2020 57% March-May
2020 0% June-Aug.
2020 0% Sept.-Nov.
2020
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions-Emission Control
GHG CAS GHG Estimation Efficiency Emission
Pollutants Pollutants Method Code (Net after Factor
(Tons/Year) (See Instructions) all controls)
2020
Criteria Emissions-Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission
Pollutants Code Pollutants Method Code (Net after Factor
(Toos/Year) (See Instructions) all controls)
2020
co co 08
NOx NOx 08
TSP TSP 08
PMlO PMl0 08
PM2.5 PM2.5 08
SO2 SO2 08
voe voe 0 08
Emissions Emission Control HAP/TAP CAS Estimation Emission
Pollutants (In Alphabetical Order) (sec instructions) HAP/TAPS Method Code Efficiency Factor
(Pounds/Year) (Net after all controls)
(See Instructions)
2020
Formaldehyde 50-00-0 0.92 08
Phenol 108-95-2 3.5 08
43%
Ef
Control
Ef
Control
EF
Control
26
Operating Scenario: OS -61 Emission Source/Group ID: G-62
10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2020)
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 Throughput:
Jan-Feb + Dec
2020 25% March-May
2020 25% June-Aug.
2020 25% Sept.-Nov.
2020
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions-Emission Control GHG CAS GHG Estimation Efficiency Emission
Pollutants Pollutants Method Code (Net after Factor
(Tons/Year) (See Instructions) all controls)
2020
Criteria Emissions-Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission
Pollutants Code Pollutants Method Code (Net after Factor
(Tons/Year) (See Instructions) all controls)
2020 co co 08
NOx NOx 08
TSP TSP 08
PMlO PMlO 08
PM2.5 PM2.5 08
SO2 SO2 08
voe voe 08
Emissions E mission Control HAP/TAP CAS Estimation Emission
Pollutants (In Alphabetical Order) (see instructions) HAP/TAPS Method Code Efficiency Factor (Pounds/Year) (Net after all controls)
(See Instructions)
2020
Methylene diphenyl
diisocyanate (MDI) 101-68-8 0.0178 08
(Component of POMTV)
25%
Ef
Control
Ef
Control
EF
Control
24
Operating Scenario: OS -84 Emission Source/Group ID: G-58
10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2020)
Hours per Day ( 22 ) Days per W eek { 7 ) Weeks per Year ( 50 )
11. Typical Start & End Times For Operating Scena rio: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throughput:
J an-Feb+ Dec
2020 25% March-May
2020 24% June-Aug.
2020 27% Sept.-Nov.
2020
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions-Emission Control
GHG CAS GHG Estimation Efficiency Emission
Pollutants Pollutants Method Code (Net after Factor
(f ons/Y ear) (See Instructions) all controls)
2020
Criteria Emissions-Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission
Pollutants Code Pollutants Method Code (Net after Factor
(f ons/Y ear) (See Instructions) all controls)
2020
co co 08 0
NOx NOx 08 0
TSP TSP 2.2 10 98 0.59
PMl0 PMlO 2.2 10 98 0.59
PM2.5 PM2.5 2.2 10 98 0.59
SO2 SO2 08 0
voe voe 9.1 10 0 2.44
Emissions Emission Control HAP/TAP CAS Estimation Emission
Pollutants (In Alphabetical On!er) (see instructions) HAP/TAPS Method Code Efficiency Factor (Pounds/Year) (Net after all controls)
(See Instructions)
2020
Formaldehyde 50-00-0 401.11 04 0
Methanol 67-56-1 901.01 04 0
24%
Ef
Control
Ef
Control
AFTER
AFTER
AFTER
AFTER
EF
Control
AFTER
AFTER
22
Polychlorinated biphenyls 1336-36-3 0.0014 08 AFTER
(PCB)
Polycyclic Organic Matter
(Inc P AH, dioxins, etc. NC POM 0.5095 08 AFTER
& AP 42 historic
amorphous elob)
Propionaldehyde 123-38-6 4776.83 04 AFTER
Propylene dichloride 78-87-5 3.8109 08 AFTER
Selenium Compounds SEC 0.65 08 AFTER
Styrene 100-42-5 219.4129 08 AFTER
Toluene 108-88-3 544.3948 08 AFTER
Trichlorobenzene, 1,2,4-120-82-1 0.0371 08 AFTER
Trichloroethylene 79-01-6 3.4644 08 AFTER
Trichlorophenol, 2,4,6-88-06-2 0.0025 08 AFTER
Vinyl chloride 75-01-4 2.0786 08 AFTER
Xylene 1330-20-7 356.5303 08 AFTER
20
IS-MDl-4 volatile organic liquid storage tank
(30,000 gallon capacity)
nail line marking (Group l
IS-N-1 miscellaneous coating operations)
[MACTDDDD]
IS-P-1 propane tank (1,500 pounds)
IS-PF-5 volatile organic liquid storage tank
(15,000 gallon capacity)
IS-PF-6 volatile organic liquid storage tank
(15,000 gallon capacity)
Printing operations consisting of the
Logo and AP A stamp operations and
Re-grade. The AP A stamp goes on
the saw line, where the Logo goes on
in the paint booth. Boards that fail
IS-PO-1 quality standards required for AP A
certification are re-graded by
covering the AP A stamp either
manually with a roller or a spray
system located between the saw line
and stacker units (Group I
miscellaneous coating operations)
IS-PP-I portable pump
stencil painting or "end stripping"
IS-SP-I (Group I miscellaneous coating
operations) [MACT DDDD)
IS-TO-1 thermal oil storage
IS-UO-1 used oil tank
IS-W-1 wax tanks
IS-W-2 waferizer
IS-W-3 welder
IS-WC-I welding and cutting torch
IS-WE-I volatile organic liquid storage tank
(12,000 gallon capacity)
IS-WE-2 volatile organic liquid storage tank
(12,000 gallon capacity)
OSB board processing operation -propane/natural gas-fired regenerative thermal
OSB press enclosure vent from one CS-11 oxidizers (24 million Btu per hour heat input RTO-3 PV-1 totally enclosed hot press [MACT rate) DDDD)
OSB board processing operation -propane/natural gas-fired regenerative thermal
OSB press enclosure vent from one CS-11 oxidizers (24 million Btu per hour heat input RTO-3 PV-2 totally enclosed hot press [MACT rate)
DDDD]
cyclone (144 inches in diameter),cyclone (144
inches in diameter),cyclone (144 inches in Wafer Drying Process -wood diameter),cyclone (144 inches in fuel/recycled resinated wood diameter),cyclone (144 inches in diameter),wet
fuel/natural gas-fired thermal oil electrostatic precipitator (22,651 square feet of PCYCD-1, heater (40 million Btu per hour heat collection area),wet electrostatic precipitator PCYCD-2, input rate) -[POS] exhausting
CS-17 (22,651 square feet of collection . PCYCD-4, WESP-TOH-1 directly to the bark burner and area),propane/natural gas-fired regenerative I, WESP-2, RTO-4, indirectly supplying heat to the thermal oxidizer (13.5 million Btu per hour RTO-5, RTO-6 presses [NSPS De, MACT DDDD]; heat input rate),propane/natural gas-fired [AOS] exhausting to stacks (atm) regenerative thermal oxidizer (13.5 million Btu while firing natural gas only [MACT per hour heat input rate),propane/natural gas-
DDDDD] fired regenerative thermal oxidizer (13.5
million Btu per hour heat input rate),
5
COPY of RECORD Date Submitted: 6/30/202111:27:35
As entered in AERO
Facility ame: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Roxboro, NC 27574
Emission Source & Operating Scenario List -See Instructions
• ES Group ID *Es ID
ORI TS-I.CO, TS-1.ADH
GR5 CP-005, CYC5
BARK.I, BARK.l.D-1,
BARK.1.D-2, BARKl.D-3,
G-56 BARK.l.D-4, BARK.LO-
4A, BARK.l.D-5, TOH-1,
TOH-2
0-58 CP-003, CP-004, CYC9
G-62 IS-MDI-4, IS-MDI-3
G-63 IS-PF-5, IS-PF-6
G-67 PV-1, PV-2
IS-CO-1, IS-CT-I, lS-O-1,
IS-DD-la, IS-O-1, IS-HH-1,
IS-HO-I, IS-HO-3, IS-PP-I,
G-74 IS-TO-I, IS-UO-1, IS-B-1,
IS-BC-1, IS-BS-I, IS-C-1,
IS-DB-I, IS-HO-2, IS-N-1,
IS-P-1, IS-SP-1, IS-DD-l b,
IS-W-2, IS-W-3, IS-WC-1
BARK. l .D-1 A
BARK.l.D-2A
BARK.l.D-3A
BARK1.D-5A
CP-001
CP-002
CP-006
CP-007
ENGi
F-1
FUELPREP
IS-DF-1
IS-EO-1
IS-PO-I
IS-W-1
*osm
79
80
87
86
84
61
62
63
85
NONE
NONE
NONE
NONE
70
2
59
7
20
21
60
33
77
78
NONE
Facility ID : 7300061
Permit: 07760
County : Person
DAQ Region : RRO
• OS Description
TechShield Cleanners
TechShield Adhesive
CP00-5, Mat reject and flying cutoff saw.
B-5, CYC5-l, CYC5-2, and CYC5
Dryer system with new RTO's Primary
Operating Scenario
Saw line baghouse and dryer screen fines
collection
Storage of MDI raw materials
Storage of phenol-fonnaldehyde resin raw
materials
Pressing OSB
Nail line and Stencil
NONE
NONE
NONE
NONE
sawtrim and finishing line clean-up with
bypass cyclone
blender and forming bin aspiration systems
Sander dust collection from tongue and
groove process
sanderdust bin transfer and loading system
diesel-fired emergency generator (1,332
horsepower)
bark handling fugitives
Wood fuel metering bin collection
diesel fire pump
Application of edgeseal to the finished
product.
Stamp ink
NONE
7
COPY of RECORD Date Submitted: 6/30/202111 :27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Roxboro, NC 27574
North Carolina Department of Environmental Quality
Division of Air Quality
Facility ID: 7300061
Permit : 07760
County : Person
DAQ Region : RRO
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
1. Emission Source ID (from permit)
or Emission Source Group ID
2. Emission Source Description :
Group GRl consisting ofTS-1.CO, TS-1.ADH
TechShield
OS -79/TechShield Cleanners 3. Operating Scenario ID/
Description:
4. sec Number/Description: 49099998/Miscellaneous Volatile Organic Compound Evaporation ; Identify
the Process and Solvent in Comments
5. Throughput/units in 2020:
( e.g. production or fuel use):
6. Fuel Information
(If fuel is used)
7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
8. Control Device Information :None
Order CS-ID CDID
(as listed in permit)
I Hat Co,rent I
(Btu/units)
Control Device Description
9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):
ERPID ERP Type Height Diameter Temperature Velocity Volume Flow
(in feet) Circle (enter#): (F) (Feel/see) Rate (Adm) Rectangle (L x W)
(in 0.1 feet)
T-lC FUGITIVE (NO 1 72 Area= 1
STACK)
ERP Description
TechShield Cleaner
9
COPY of RECORD Date Submitted: 6/30/202111 :27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Roxboro, NC 27574
North Carolina Department of Environmental Quality
Division of Air Quality
Facility ID : 7300061
Permit: 07760
County : Person
DAQ Region : RRO
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
1. Emission Source ID (from permit)
or Emission Source Group ID
2. Emission Source Description :
Group GRl consisting ofTS-1.CO, TS-1.ADH
TechShield
OS -80/TechShield Adhesive 3. Operating Scenario ID/
Description:
4. SCC Number/Description: 49099998/Miscellaneous Volatile Organic Compound Evaporation ; Identify
the Process and Solvent in Comments
5. Throughput/units in 2020:
(e.g. production or fuel use):
6. Fuel Information
(If fuel is used)
7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
8. Control Device Information :None
Order CS-ID CDID
178200 GAL/yr
¾Sulfur
(as listed in permit)
¾Ash Heat Content
(Btu/units)
Control Device Description
9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):
ERPID ERP Type Height Diameter Temperature Velocity Volume Flow
(in feet) Circle (enter#): (F) (Feet/sec) Rate (Acfm) Rectangle (L x W)
(in 0.1 feet)
T-1 FUGITIVE (NO
STACK) 1 72 Area= 1
ERP Description
Fugitive emissions
from abesive
11
COPY of RECORD Date Submitted: 6/30/2021 11:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Facility ID : 7300061
Permit : 07760
County : Person Roxboro, NC 27574
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
1. Emission Source ID (from permit)
or Emission Source Group ID
2. Emission Source Description :
3. Operating Scenario ID/
Description:
4. SCC Numberillescription:
5. Throughput/units in 2020:
(e.g. production or fuel use):
6. Fuel Information
(If fuel is used)
7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
8. Control Device Information :None
Order CS-ID CDID
Group GRS consisting ofCP-005, CYC5
OSB fonning process -mat reject and flying cut off saw system
OS -87/CP00-5, Mat reject and flying cutoff saw. B-5, CYC5-l, CYC5-
2, and CYC5
30700803/Sawmill Operations ; Sawdust Pile Handling
7455.2 HR/yr
I H<MCootmt I
(Btu/units)
Control Device Description
(as listed in permit)
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 Vol ume Flow ERP Description
(in feet) Circle (enter #): (F) (Feet/sec) Rate (Acfm) Rectangle (L x W)
(in 0.1 feet)
VERTICAL circular stack for
CP005 STACK 43 4.8 75 31.5 34200.63 mat reject line and
saw system
13
COPY of RECORD Date Submitted: 6/30/202111:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Facility ID : 7300061
Permit: 07760
County : Person Roxboro, NC 27574
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
1. Emission Source ID (from permit)
or Emission Source Group ID
2. Emission Source Description :
3. Oper ating Scenario ID/
Description:
4. SCC Number/Description:
5. Throughput/units in 2020:
(e.g. production or fuel use):
6. Fuel Information
(If fuel is used)
7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
8. Control Device Information :
Order CS-ID CDID
Group G-56 consisting of BAR.Kl, BAR.Kl.D-1, BAR.Kl.D-2,
BARK.1.D-3, BAR.Kl.D-4, BARK.1.D-4A, BARK.l.D-5, TOH-1, TOH-2
One bark burner, five natural gas fired dryers and two wood-fired
thermal heaters
OS -86/Dryer system with new RTO's Primary Operating Scenario
30701020/0riented Strandboard (OSB) Manufacture ; Direct Natural Gas-
fired Rotary Dryer, Hardwoods
356270 TON/yr
I u~, Cootoot I
(Btu/umts)
Control Device Description
(as listed in permit)
1 CS-17 PCYCD-1 One cyclone (144 inches in diameter)
2 CS-17 PCYCD-2 One cyclone (144 inches in diameter)
3 CS-17 PCYCD-4 One cyclone (144 inches in diameter)
4 CS-17 WESP-1 One wet electrostatic precipitator (22,65 1 square feet of collection
area)
5 CS-17 WESP-2 One wet electrostatic precipitator (22,651 square feet of collection
area)
6 CS-17 RTO-4 One propane/natural gas-fired regenerative thermal oxidizer (1 1
million Btu per hour heat input rate)
7 CS-17 RTO-5 One propane/natural gas-fired regenerative thermal oxidizer (11
million Btu per hour heat input rate)
8 CS-17 RTO-6 One propane/natural gas-fired regenerative thermal oxidizer (11
million Btu per hour heat input rate)
15
Operating Scenario: OS -86 Emission Source/Group ID: G-56
9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feel} Circle (enter#): (F) (Feel/sec} Rate (Adm) "Rectangle (L x W}
(in 0.1 feel}
Dryer VERTICAL l 10 9.5 250 64.66 275000 Dryer RTO
RTO STACK common stack
17
Methylene Diphenyl Diisocyanate Tank Emissions
Equation:
Emissions are based on AP-42, 5th Edition Chapter 7. These tanks are located in ate
controlled environment. Therefore, the temperature of these tanks does not vary. As,
the tanks do not have any breathing loss. The storage tank emission calculation proce
then simplifies to the equation below.
Lw = 0.0010 * Mv * PvA • Q • KN • Kp
Lw
Mv
PvA
Q
KN
Kp
N
where:
where:
HLX
D
therefore:
LP Roxboro
Working Loss, lbs/yr
Vapor Molecular Weight, lb/lb-mol
Vapor Pressure at Daily Average Liquid Surface Temperature, psia
Annual Net Throughput, bbl/yr
Turnover Factor, dimensionless, (180 + N)/6N for N >36 else 1
Working Loss Product Factor Is 1 Unless a Crude Oil Then 0.75
Number of Turnovers
N = 5.614Q/VLX
Tank Maximum Liquid Volume, cu. ft
VLX = pi • D2/4 • HLX
Maximum Liquid Height, ft
Tank Diameter, ft
N = 5.614 * Q /(pi • D2/4 • H)
Facility ID: 7300061 Permit No. 07760T24
Methylene Diphenyl Diisocyanate Tank Emissions
Basis:
Number of Tanks
Actual Throughput
Maximum Annual Throughput
Tank Size
Tank Diameter
Tank Height
Tank Shell Height
Tank Liquid Height
Fill Rate
Maximum Fill Rate
Material Classification (Crude Oil or VOC)
Conversion Factor (Gallons per Barrel)
MDI Specific Gravity
MDIMv
MDI PvA
Oactual hourly
48000 gal/hr I 42 gallons/bbl =
Oactual annual
1637977.61790568 gallons/yr/ 42 gallons/bbl=
Omaxhour1y
48000 gal/hr/ 42 gallons/bbl =
Omax annual
1854400 gallons/yr/ 42 gallons/bbl =
Noe1uol
5.614 • 38999 bbl/yr/ (2 tanks• pi • 12 ftA2 • 32 ft)=
Nm.,.
5.614 * 44152 bbl/yr/ (2 tanks* pi* 12 W2 * 32 ft)=
KN actual
Since N < or equal to 36 the value is
KN max
Since N < or equal to 36 the value is
Kp
Materials other than crude oil have a value of
2 tanks
1,637,978 gallons/yr
1,854,400 gallons/yr
30,584 gallons
12 ft
34 ft
32 ft
32 ft
48,000 gal/hr
48,000 gal/hr
voe
42 gallons/bbl
1.2
236 lb/lb-mol
1.93E-06 psia
1143 bbl/hr
38999 bbl/yr
1143 bbl/hr
44152 bbl/yr
8
9
LP Roxboro Facility ID: 7300061 Permit No. 07760T24
Methylene Diphenyl Diisocyanate Tank Emissions
Emission Calculations:
Pollutant
Name
voe
MDI
(lbs/hr)
Actual Emissions
(lbs/vrl
0.0005
0.0005
0.0178
0.0178
voe Actual Emissions (lbs/hr)
(tons/vr'
0.000009
0.000009
0.0005 lbs/hr formaldehyde* 1 lb VOC/lb formaldehyde =
voe Actual Emissions (lbs/yr)
0.0178 lbs/hr formaldehyde• 1 lb VOC/lb formaldehyde=
voe Actual Emissions (tons/yr)
0.0178 lbs/yr/ 2000 lbs/Ion =
MDI Actual Emissions (lbs/hr)
0.0005 lbs/hr
0.0178 lbs/yr
0.000009 tons/yr
0.001 * 236 lb/lb-mol * 0.00000193 psia * 1143 bbl/hr* 1 * 1 =
0.0005 lbs/hr
MDI Actual Emissions (lbs/yr)
0.001 * 236 lb/lb-mol * 0.00000193 psia * 38999 bbl/yr* 1 * 1 =
MDI Actual Emissions (tons/yr)
0.0178 lbs/yr / 2000 lbs/ton =
LP Roxboro
0.0178 lbs/yr
0.000009 tons/yr
Facility ID: 7300061 Permit No. 07760T24
COPY of RECORD Date Submitted: 6/30/202111:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Facility ID : 7300061
Permit : 07760
County : Person Roxboro, NC 27574
DAQ Region : RRO
Listing of Emission Sources and Control Devices on Permit. See instructions
• ES ID on • ES Description •csm • CS Description • CDID's
Air Permit
cyclone (144 inches in diameter),cyclone (144
inches in diameter),cyclone (144 inches in
diameter),cyclone (144 inches in
Wafer Drying Process -one diameter),cyclone (144 inches in diameter),wet
bark/wood ( dry and wet)-electrostatic precipitator (22,651 square feet of PCYCD-1,
fueVrecycled resinated wood fuel-collection area),wet electrostatic prccipitator PCYCD-2,
BARK.I fired burner (190 million Btu per CS-17 (22,651 square feet of collection PCYCD-4, WESP-
hour maximum heat input rate) area),propane/natural gas-fired regenerative l, WESP-2, RTO-4,
providing direct heat direct fired thermal oxidizer (13.5 million Btu per hour RTO-5, RTO-6
wafer dryers [MACT DODD] heat input rate),propane/natural gas-fired
regenerative thermal oxidizer (13.5 million Btu
per hour heat input rate),propane/natural gas-
fired regenerative thermal oxidizer (13.5
million Btu per hour heat input rate),
cyclone {144 inches in diameter),cyclone (144
inches in diameter),cyclone (144 inches in
diameter},cyclone (144 inches in
diameter),cyclone {144 inches in diameter),wet
electrostatic precipitator (22,651 square feet of PCYCD-1,
Wafer Drying Process -triple pass collection area),wet electrostatic precipitator PCYCD-2,
BARK.1.D-1 direct-fired wafer dryer [MACT CS-17 (22,651 square feet of collection PCYCD-4, WESP-
DODD] area),propane/natural gas-fired regenerative 1, WESP-2, RTO-4, thermal oxidizer {13.5 million Btu per hour RTO-5, RTO-6 heat input rate),propane/natu.ral gas-fired
regenerative thermal oxidizer (13.5 million Btu
per hour heat input rate),propane/natural gas-
fired regenerative thermal oxidizer (13.5
million Btu per hour heat input rate),
BARK.l.D-Wafer Drying Process -single--pass
IA direct fired wafer dryer [MACT
DODD]
cyclone (144 inches in diameter),cyclone {144
inches in diameter),cyclone (144 inches in
diameter),cyclone {144 inches in
diameter),cyclone (144 inches in diameter),wet
electrostatic precipitator (22,651 square feet of PCYCD-1,
Wafer Drying Process -triple pass collection area),wet electrostatic precipitator PCYCD-2,
BARKI.D-2 direct-fired wafer dryer [MACT CS-17 (22,651 square feet of collection PCYCD-4, WESP-
DODD] area),propane/natural gas-fired regenerative 1, WESP-2, RTO-4, thermal oxidizer (13.5 million Btu per hour
heat input rate),propane/natural gas-fired RTO-5, RTO-6
regenerative thermal oxidizer (13.5 million Btu
per hour heat input rate),propane/natural gas-
fired regenerative thermal oxidizer (13.5
million Btu per hour heat input rate),
2
Facility Total CY 2020 Emissions Summary
COPY of RECORD Date Submitted: 6/30/202111:27:35
As entered in AERO
Facility Name: Louisiana-Pacific Corporation -Roxboro
10475 Boston Road
Roxboro, NC 27574
North Carolina Department of Environmental Quality
Division of Air Quality
Facility ID : 7300061
Permit : 07760
County : Person
DAQ Region : RRO
Air Pollutant Point Source Emissions Inventory -Calendar Year 2020
Record Facility-Wide Totals From all Permitted and Non-Permitted AirPollutant E mission Sources
Green House Gases Pollutants GHG
Actual Emissions (TonsNear)
Pollutant CAS 2020 2019
Criteria Pollutants
Actual Emissions (Tons/Year)
Pollutant CAS 2020 2019
co co 116.33 101.77
NOx NOx 141.26 135.49
PM(TSP) TSP 68.l 66.3
PMIO PMIO 66.38 64.6
PM2.5 PM2.5 66.38 64.6
S02 S02 6.84 8.81
voe voe 129.9 127.85
Hazardous Air Pollutants(HAPS) and/or Toxic Air Pollutants(TAPs)
I I Actual Emissions (Pounds/¥ ear)
Pollutant ICAS 12020 12019
Pollutant Group:Antimony & Compounds (total mass, inc elemental SB) Group Sum: 1.8246
Antimony Unlisted Compounds I SBC-Other 11.8246 12,1364 (Specify & Component of SBC)
% Change
% Change
14.306775%
4.258609%
2.714925%
2.7554162%
2.7554162%
-22.360956%
l.603438%
I
I% Change
1-14.5946455%
Pollutant Group:Arsenic & Compounds (total mass of elemental AS, arsine and all inorganic compounds) Group Sum:4.70017
Arsenic Unlisted Compounds ( IASC-Other 14,70017 14,66027 I 0.8561698% Specify & Component of ASC)
Pollutant Group:Beryllium & compounds (Total mass) Group Sum:.25423
Beryllium metal (unreacted) 17440-41-7 jo.25423 I .29771 1-14.60482% (Component ofBEC)
Pollutant Group:Cadmium & compounds (total mass inc elemental metal) Group Sum: 1.18473
Cadmium Metal ( elemental 17440-43-9 11.18473 11.32661 1-10.694923% unreacted, Component of CDC)
Pollutant Group:Chromium (VI) Soluble Chromate Compounds (Component ofCRC) Group Sum:.9434
Chromic acid (VI) (Component of 17738_94_5 SolCR6 & CRC) 10,9434 I 1.0505 1-10.195146%
PolJutant Group:Chrornium -AIVfotal (Inc Chromium (VI) categories, metal and Others) Group Sum: 14.8054
57
Methyl isobutyl ketone 108-10-1 788.61 776.55 1.5530227%
Methylene chloride 75-09-2 217.347 221.168 -1.7276455%
Nitrophenol, 4-100-02-7 0.0127 .0149 -14.7651005%
Pentachlorophenol 87-86-5 0.0059 .0066 -10.606057%
Perchloroethylene 127-18-4 ( tetrachloroethylene)
4.3883 5.14 -14.624512%
Phenol 108-95-2 7946.241 7858.2 1.1203712%
Polychlorinated biphenyls (PCB) 1336-36-3 0.0014 .0016 -12.500001%
Polycyclic Organic Matter (Inc
PAH, dioxins, etc. NC & AP 42 POM 0.60265 .66604 -9.517448%
historic amorphous glob)
Propionaldehyde 123-38-6 5969.65 5904.77 1.0987707%
Propylene dichloride 78-87-5 3.8109 4.4621 -14.594026%
Propylene oxide 75-56-9 0.2886 .255 13.176472%
Selenium Compounds SEC 0.65063 .76103 -14.506658%
Styrene 100-42-5 444.1329 479.3015 -7.3374705%
Toluene 108-88-3 743.94904 738.86181 0.6885211%
Trichlorobenzene, 1,2,4-120-82-1 0.0371 .0434 -14.516134%
Trichloroethylene 79-01-6 3.4644 4.0565 -14.596325%
Trichlorophenol, 2,4,6-88-06-2 0.0025 .003 -16.66667%
Vinyl acetate 108-05-4 1378.402 1135.90531 21.34832%
Vinyl chloride 75-01-4 2.0786 2.4339 -14.597977%
Xylene 1330-20-7 581.2772 570.55249 1.8797098%
59
Louisiana Pacific Roxboro's Air Emissions Inventory -Toxic Compliance 2020
IOUII
TPER In
Pollutant (Iba/yr) TPER limit TPER limit (2nd) 2020 TPER Emissions Compliance
IAcetaldehyde 19,923.67 6.80 lb/hr 2.54 lb/hr yes
benzo (a)pyrene 0.601 2.20 lb/yr 0.6008 lb/yr yes
carbon Tetrachloride 5.20 460 lb/yr 5.20 lb/yr yes
Chlorine 91.23 0.23 lb/hr 0.79 lb/day 0.28 lb/day yes
Chlorobenzene 3.81 46 lb/day 0.01 lb/day yes
Chloroform 3.23 290 lb/yr 3.23 lb/yr yes
ldi(2-ethylhexyl)phthalate 0.0543 0.63 lbs/day 0.00 lb/day yes
Ethylene dichloride 3.3489 260.00 lb/yr 3.35 lb/yr yes
n-hexane 389.02 23.00 lbs/day 1.19 lb/day yes
Mercury, aryl and
inorganic compounds 0.86 0.013 lb/day 0.003 lb/day yes
1, 1, 1-Trichloroethane 3.58 250 lb/day 64 lbs/hr 0.01 lb/day yes
Methyl ethyl ketone 317.14 22.4 lb/hr 78 lb/day 0.97 lb/day yes
methyl isobutyl ketone 788.61 7.6 lb/hr 52 lb/day 2.42 lb/day yes
Chloromethane 2.66 1600 lb/yr 0.39 lbs/hr 0.00 lb/hr yes
Nickel 21.13 0.13 lb/day 0.06 lb/day yes
Pentachlorophenol 0.006 0.0064 lb/hr 0.063 lbs/day 0.0000 lb/hr yes
Styrene 444.13 2.70 lb/hr 1.43 lb/hr yes
ITCDD-2378 4.66E-10 0.00020 lb/vr 0.0000 lb/yr yes
perchloroethylene 4.39 13000 lb/yr 4.39 lb/yr yes
Toluene 743.95 14.40 lb/hr 98 lb/day 2.28 lb/day yes
Trichloroethylene 3.46 4,000 lb/yr 3.46 lb/yr yes
Mnyl Chloride 2.08 26 lb/yr 2.08 lb/yr yes
Xylene 581.28 16.40 lb/hr 57 lb/day 1.87 lb/day yes
lJryer uryer 1ns19m11cant 11ns19m11can1 t't-t't-
RTO's RTO's RT0#3 RT0#3 Sources Sources CP002 CP002 CP003/ Tanks Tanks CP005 CP005 TechShiel TechShield
Pollutant Limit Actual limit Actual Limit Actual Limit Actual CP003I4 Limit 4 Actual Limits Actual Limit Actual d Limit Actual•
Acrolein I lbs/hr) 20.32 0.62 2.44 0.16 NA NA NA NA NA NA
!Arsenic Obs/hr) 0.0012 0.0006 NA NA NA NA NA NA NA
Benzene Obs/hr) 0.60 0.03 0.24 0.00 0.12 332.80 NA NA NA NA NA
Benzene 0bs/vr) NA 332.80 0.12 NA NA NA NA NA
Bervllium Metal (lbs/hr\ 0.02 0.00 NA NA NA NA NA NA NA
Cadmium Metal Obs/hr\ 0.03 0.00 NA NA NA NA NA NA NA
Chromium (VI) (lbs/hr\ 0.00042 0.00010 NA NA NA NA NA NA NA
Formaldehyde (lbs/hr\ 6.54 0.42 7.5 0.17 NA 1.9 0.42 0.16 0.05 0.27 0.00 0.095 0.029 0.27 0.0663
Hvdrooen Chloride /lb/hr\ 182.54 0.05 NA NA NA NA NA NA NA
Manaanese (lbs/hr\ 23.81 0.00 NA NA NA NA NA NA NA
Phenol (lbs/hr) 2.06 0.24 17.30 0.73 NA 0.79 0.08 NA 3.18 0.00 0.018 0.0011 NA
Permij No. 07760T23
LP Roxboro Facility ID: 7300061
Calendar Year
Hours of Operation
!Total DNer RTO's
Dryer RTO's (4-6) (POS)
Drver RTO's 14-6) (AOS)
Single Pass Drver
RT0-3 I Press
B-1, B-2, B-3, B-5
B-6, B-7
B-8
IT&G Production
!Tech Shield
F~e Pump
Emeraency oenerator
Production Data • All Products -. ---
TvM lbs/ft'
7/16RS 41.36
15/32 RS 42.6
112 RS
19132 RS 41.3
Superstruc Basic 19/32 42.00
23/32TN250 39.24
23132 TN350 38.25
23/32 Laoacy 41.65
Superstruc Basic 23132 42.00
Superstruc Advan 23132 45.00
Totals
Production Data . T&G
Tvoa
23132 TN250 I
23132 TN350 I
23132 Laoacv I
Total TFP
Annual Average Production Rate
.!l'.e!
Al
TechShleld
.!...
All
Louisiana Pacific Roxboro's Air Emissions Inventory
User Input
2020
7,830.9
4,872.2
2,958.7
13,707.9
7,455.2
7,455.2
6,167.4
5,362.1
6,167.4
4,029.9
21.8
11.1
Bd-Ft (318 inch) TFP
301,629,688 194,928.3
15,761,760 10,491.4
0.0
17,611,326 11,364.8
127,680 83.8
32,462,752 20,122.7
109,052,384 70,455.1
33,230,400 23,403.4
556,416 365.1
283,360 199.2
510,715,968 331,413.8
lbs/ff' Board-Feet (318 inch basis)
39.2 32,462,752
38.3 109,052,384
41.7 33,230,400
174,745,536
Boald-Feet (318 inch basis
68,505
Board-Feet
110,251,307
Usage Data
Hours of Bypass !Total Mill Gas Consumplion (Therms)
Drver RTO's (4-6) (POS) o.c !Total Mill Gas Consumotion (mmsct)
Dryer RTO's (4-6) (AOS) o.c Dryer RTO's Gas Consumpticn (mmsci)
RT0-3 0.( Press RTO Gas Consumption (mmsci)
Drvers 33.C ITOH's Gas Consumction (mmscf)
WESP Bypass 33.C rTotal Wafer throughput throuah driers l(onsl
Bark Burner Idle 586.E IINood Fuel consumed by Bark Burner (tons)
CP001 3.92 Green Wood Fuel consumed by Bark Burner (Ions)
CP003 0.AI Resinated Wood Fuel consumed by Bark Burner (tons!
CP005 0."' !Wood Fuel consumed bv TOH (tons)
CP006 0.1( Parts Washer fluid
CP007 0.1( Nail line Ink Usage (gals)
CP008 0.1( Stencil Paint and End Strip (gals}
Nail Line and stencil
Stamp Ink (APA, Loool
Ink Jet Ink and Cleaner
Orange Edoeseal (galsl
Greys and Black Edgeseal (aalsl
Clear Edaeseal
!Total Ed<leseal Usage
ITechShield Glue (aal)
Misty Mean Green (gall
PF Consumotion (lbs. l
MDI Consumption (lbs.)
TFP
19,903.7
65,175.8
21,625.7
106,705.3
The cells in red are user input. All other cells are either calculated values 0< are constants.
LP Roxboro Facility ID: 7300061
216.12
112.91
96.7!
6.41
356,271
116,307
115,877
4"
6,511
(
6,751
3,375
10,125
4,245
0
155,2"'
18,90(
12,151
186,300
178,'°'
(
(
16,392,A8!
Permit No. 07760T24
' ,
/ ,
I
Louisiana Pacific Roxboro's Air Emissions Inventory
Source Emissions Using Permit Emission Rates
2020
RTO's 4-6 (Primary Operating Scenario)
Hours of O eration: 4 ,872
CO( ) NOx (tpy VoeWPP1 ( TSP ( PM-10 (tp )
40.61 81.68 16.48 15.32 15.32
RTO's 4-6 (Alternate Operating Scenario)
Hours of O eration: 2,959
co (tpy) NOx (tp ) VOCWPP1 ( TSP(tpy)
53.91 40.43 8.46 9.56 9.56
Single Pass Dryer Outlet (Alternate Operating Scenario)
Hours of O erations: 13,707.9
co (tp ) NOx( VoeWPP1 ( TSP (tpy)
11.30 8.48 1.80 2.01
Dryer Bypass
Hours of B ass: 33.0
CO ( NOx voe WPP1 (tp ) TSP tp ) PM-10 (tp )
0.62 0.00 1.66 0.29 0.29
Dryer RTO Bypass
Hours of B ass: 0.0
CO( ) NOx(tp ) voe WPP1 (tp > TSP PM-10 (
0.00 0.00 0.00 0.00 0.00
WESP Bypass
Hours of B ass: 33.0
c o tp) NOx (t voe Ad ustad (
0.00 0.00 0.00
Bark Burner Startup/Shutdown/Idle
Hours: 587
co NOx voe Ad ustad ( PM-10 (
3.98 3.25 0.11 2.39
Press
Press O eration: 7,455
co NOx VoeAdustad TSP ( PM-10 (tpy)
5.58 6.82 4.65 20.45 20.45
Press Bypass
Hours of B ass 0
CO( NOX t VOCAdustad PM-10
0.00 0.00 0.00
LP Roxboro Facility ID No. 7300061 Permit No. 07760T23
Emissions from Baghouse Controlled Processes
I I I Hours of Operation I voe (!Ell
CP-001 w/ 8-1 & CYC-1 7,455.2 8.50
CP-002 w/ 8-2 7,455.2 25.42
003 & CP-004 w/ 8-3 & CY 7,455.2 8.41
CP-005 w/ 8-5 & CYC-5 7,455.2 7.14
CP-006 w/ 8-6 & CYC-6 6,167.5 4.55
CP-007w/ 8-7 6,167.5 0.08
UELPREP w/ 8-8 & CYC-5,362.1 12.33
1,337 HP Diesel Fired Emergency Generator
Hours of O eration: 11 .1
PM
Actual Emissions (tons/yr) 0.005
Printing Operations -APA, Logo,
Ink Usa e als : 4,245
voe
Actual emissions (tons/yr) 0.13
Edgeseal
Usa e als : 186,300
I I PM I Actual emissions (tons/yr) I 1.16
TechShield
Usa e als :
Actual emissions (tons/yr)
LP Roxboro
178,200
voe
1.10
PM-10
0.005
PM-10
1.16
I voe Adjusted !!El} TSP(tpy)
9.09 4.40
51.06 2.16
9.09 2.20
7.72 0.48
5.03 3.27
0.56 0.06
12.68 1.77
PM-2.5 NOx
0.005 0.178
Nail line -Black Ink+ Stencil
lnk Usae als: 10,125
I I WC I Actual emissions (tons/yr) I 0.01
voe
0.25
Facility ID No. 7300061
I PM-10 !tpy) I
4.40
2.16
2.20
0.48
3.27
0.06
1.77
voe co
0.005 0.041
Permit No. 07760T23
Roxboro Emission Factors Required by
Permit 07760T24
Dryers and Thermal 011 Heaters
Dryer Outlet (Prlmarv Ooeratlno Scenario)
Eml■-lon Factor TutedPreu
Pollutant flb1.niourl Production Rat•
PMIPU-10 6.eo 71917
NOx 35_2 71 917
17_50 71917 -···~~~11 7_1 71917
Dryer Outlet (Alternate Operating Scenario)
Emlulon Factor Teated Press
Pollutant llbs~~ Production Rate
.......... 10 8_87 70886
NO,, 28.2 70686 = 37,6 70,686
•n••-11 6.0 70686
Adlustments Made for Drver t#4
Eml11k>n Factor THted Press
Pollutant llba.lhourl Production Rate
PMIPM-10 0_30 706861 NOx ,_28 706861
1.70 708861
vrY l'IV-""1) 0.27 708861
RTO#3
Emla■lon Factor Tested Press
Pollutant llba.lllour) Production Rate
PMIPM-10 6.e 82 433 --2.2 82433
1.8 82433
1l 1.S 82433
Uncontrolled Emissions:
Test Data
7119/2017
7119/2017
7/19/2017
7119/2017
Teat Date
7118/2017
7118/2017
7118/2017
7118/2017
Test Date
Tut Date
7/20/2017
7/20/2017
7/20/2017
7/20/2017
Emlsalon Factora (lballltl
units co I PII Pll-10
rlNer RTO Bvoass (POSl" 167 14.4 14,4
RTQt3•• 13.2 13.2
Bari< Bumer 13.58 9.05 6.14
WESP bvoass--•• 2,4 2,4
Orvw Bvn.oss !POSJ-37.4 17.28 17.28
I voe
I 139.8
I 82,1
I 0.385 -I 100.5
• Excura,ona -is time omisllon1occured wti.n RTO ~ 1841 and 1840". Bypass
though dr,w abort cyclonu accounted fo, as dr,w bypass It also Include• trne RTO hao
fiamed out. avtn W Temp la 1bov1 required averoga
·• Excurolon1 lime Is only time eml11lons occurred when RTO below 14S2". Bypass !hough
dryer abort cyclones accounted fo, es dryer bypass .
-Al adpulated in permit, dryer lffliHions divided by 5 (nunber of dryo,s).
-Bypau pw grid-
LP Ro>Cbolo
Baghouse Controlled Proee1H1
Emission Factors (lblhrl . ..,.. . ..,..
Units (C) IPI YOCCA4) ,__,,... -..... TSP Pll-10
CP-001 w/8-1 & CYC-1 1.87 2.28 2.44 0.050 0 1514 1.18 1.18
CP-002 w/B-2 S.S9 8.62 13.70 0,558 9.0000 0,58 0.58
CP-003 &CP004 w/B-3 & CYC-3 1.8S 2.28 2.44 0.071 0.1586 O.S9 0.59
CP--005 w/B-5 & CYC-5 1.57 1.92 2.07 0050 0.1514 0.13 0.13
CP-008 wlB-8 & CYC-8 1.21 1.48 163 0.050 0.1514 1.08 1.08
CP~7wJB.7 0.02 002 018 0050 01514 0.02 0.02
FuelPrep w/S-8 & CYC-8 3.TT 4 60 4.73 0029 01440 0.66 0.88
Diesel-Fired Emergency Generator (1337 hol
I CO I N0x I PIIIPll-10 I voe
Emission Factor I 7.35 I 32 09 I 0.9◄ I 094
Emission Factor Units I lblllr I lb/hr I lb/II,' I lblllr
Misc. Operations
Edgeaeal
lvoc l P11I Pll-10
Emiuion Factor fib/a.an I 0.00281 0.013 I 0.012S
Black Logo, APA, Regrade,
I voe I I
Eminion Factor {lb/gal) I 0.081 I I
Nall line · Black Ink♦ Stanciel
I voe I I
Emlnion Factor (lblaal) I o.002el
TechShleld voe
Emiuion Factor Jbl al 0.0123
Faciity 10: 7300081 Permrt No. 0TT80T24
Stack Test Emission Factors
Emission Factors Developed from Stack Testing
-•i -•--··-···--····-· -··. -------
MEK Phenol Autaldenvae Acroleln Methanol Chromium
Emission Factor 0.0003 0.24 2.39 0.61 0.62 0.42 0.00175
Emission Factor Units lb/ODT lbs/hr lbnlr lb/hr lb/hr lb/hr lbnlr
llerane AnMllc: -··-Chromium Nickel LHd Forma........,. U
Emission Factor 0.03 0.0006 0.00006 0.00175 0.00267 0.0006 0.0028 0.42 I
Emission Factor Units lblhr lb/hr lblhr lblhr lb/hr lblhr lbshlr lb/hr I
Basis for Emission Rates:
1. The emission factors for MEK are based on NCASI stack testing for panel plants.
2. All metals, Acetaldehyde, Propionaldehyde, Acrolein, Phenol, and Benzene based on MACT testing conducted 8130/2006
3. The emission factors for formaldehyde and Methanol are based on MACT Stack testing conducted 7/2017.
Press
1 Methanol MDI-REG PflellCII Acetal Acrolelii a.nnc.
-Eriiiiiloni= actor 0.0025 0.0025 0.00067 0.0107 G.15 0.16 0.16 0.004
-Emission Factor Units lb/MSF lb/MSF lb/hr lb/MSF lb/hr lb/hr lb/hr lb/hr
Basis for Emission Rates:
1. The emission factors for formaldehyde and Methanol are based on MACT Stack testing conducted 7 /2017.
2. The emission factor for MDI, Acetaldehyde, Propionaldehyde, Acrolein, and Benzene is based on MACT stack testing conducted 8/2006.
3. The emission factor for Phenol is based on NCASI stack testing for panel plants
Emission Factors from Baghouse Controlled Processes lbs/MSF or lb 1/hr)
Methanol MDI Forma-Phenol
Unlls 111/MSF 1111hr 111/MSF lllltlour
CP-001 w/ B-1 & CYC-1 ----
CP-002 w/ S-2 0.1000 0.0028 0.0062 0.0792
l>-003 & CP-004 wl 8-3 & CYC 0.0018 -0.0008 -
CP-005 wl S-5 & CYC-5 -0.000037 0.00042 0.0011
CP-006 w/ 8-6 & CY~ ----
CP-007w/ 8-7 0.0016 ---
FUELPREP w/ 8-8 & CYC-8 0.0016 -0.0003 -
Basis for Emission Rates:
NCASI Database, Emission Factor Database (2009) used, which includes site specific tests.
CP-002-Baghouse tested in NCASI TB 772 410-1BL1; Formaldehyde and methanol are three run average plus two standard
deviations. MDI estimated from Hanceville aspiration baghouse tests.
CP-003 -Baghouse tested in NCASI TB 772 410-1WD1. Methanol is average of three BP values plus two standard deviations.
Formaldehyde is average of one BP value and two DU2 values plus two standard deviations
CP-005 -NCASI database (Index# 2209 and 2207). MDI and Phenol emissions estimated from testing at LP Hanceville plant.
CP-007 -Methanol estimated to be equal to that from FUELPREP.
CP-008 -Methanol is average of one BP value and two DL/2 values plus two standard deviations. Formaldehyde is
average of three DL/2 values plus two standard deviations.
LP Roxboro Facility 10: 7300061 Permit No. 07760T24
Stack Test Emissions
Louisiana Pacific Roxboro's Air Emissions Inventory
Facility Em issions
Dryers and TOH's
Press
Production M brd-ft 3/8"
Oven Dried Tons (ODT)
Press Operation
-----fl -----------•;:::)I·--
CP-001 w/ B-1 & CYC-1
CP-002 w/ B-2
CP-003 & CP-004 w/ B-3 & CYC-3
CP-005 w/ 8-5 & CYC-5
CP-006 w/ B-6 & CYC-6
CP-007w/ B-7
FUELPREP w/ B-8 & CYC-8
MEK
234.93
510,716
356,270
7,455
1,301.06
-----------C 111
Hours of Operation
7,455.2
7,455.2
7,455.2
7,455 .. 2
6,167.4
6 167.4
5,362.1
Phenol-Formaldehyde Tanks
Phenol
.. ------
MSF llellllnol•-
510,716.0 0.00
510,716,0 51,071.60
510,716.0 901.04
510,716.0 0.00
174,745.5 0.00
174,745.5 279.59
174,745,5 279.59
I I voe CIDM/YIJ I Formaldehclye l'!i:T? I Phenol (lbalyr) ~ Actual Emissions O 0.00 0.00
MDI Tanks I Actual Emis~ns I v~oF. I ~imr I
Chromlum(II
13.70
IIDl 1maivn
0
20.87
0
0.276
0
0
0
LP Roxboro Facility ID No. 7300061
Leld(II
4.70
1,192.82
Form■-1 -,vn Phenol 1maivn
0 0
3,166.4 590.45
401.11 0
214.50 8.20
0 0
0 0
57.12 0
Chromium
13.70
Bel1Z811e
29.82
Permit No. 07760T24
LP Roxboro
Spreadsheet Emissions
Spreadsheet Developed Emissions
Pollutant
NOx co
PM10
TSP
S02 voe
Pollutant
Cadmium
Carbon Tetrachloride
Chlorine
Chlorobenzene
Chloroform
Chloromethane
alt
Oichlorobenzene
1,2-Oichloroethane
Pentachloro henol
Phenol
Po lorinated bi hen
POM
Selenium
S ene
TCOD-2376
etrachlorethene
Toluene
Trichlorobenzene
1 1, 1-Trichloroethane
ol
3.33E-05
1.65E-01
5.42E-02
2.29E-02
4.90E-03
1.56E-01
6.54E-02
4.69E-01
8.23E+00
3.44E-01
2.92E-01
2 <40E-01
1 35E-01
7.29E-02
1.76E-03
3 02E-01
3.02E+OO
3<4<4E-01
2 19E-02
1.88E-03
9.81E-03
3.23E-01
7.29E-02
5.63E-02
1.01E+00
1.15E-03
5.31E-04
Stack Test Data Used
1.66E+00
Stack Test Data Used
Stack Test Data Used
5.46E-01
2.31E-01
4.94E-02
1.56E+00
8.62E-01
4.73E+0O
8.30E+01
3.47E+00
2.94E+00
2.42E+00
1.37E+OO
7.35E-01
Stack Test Data Used
1.77E-02
3.05E+00
3.05E+01
3.47E+OO
2.21E-01
1.69E-02
0.74
Included with d
1.02E+01
Stack Test Data Used
1.16E·02
5.32E-03
Stack Test Data Used
1.25E-04 1.26E-03
3.89E-02 3.92E-01
5.83E-02 5.66E·01
1.96E+01 2.00E+02
2.47E-11 4.41E-10
3 96E-01 3.99E+OO
9.56E+O0 Included with d
3.34E-03 3.37E-02
3.23E-01 3.26E+00
3.13E-01 3.15E+O0
2 29E-04 2.31E-03
1.68E-01 1.69E+OO
Pollutants In red are federally regulated HA sonly.
Pollutants In purple are NC regulated TAPs only.
All other pollutants are both HAPs and T APs.
Facili1y 10: 7300061 Permit No. 07760T24
LP Roxboro
Press RTO
MMSCF Natural Gas
l'otlutallta
NG Combustion
"V2
Benzo(aJpyrene
Cadmium
Chromium
Dichlorobenzene
Hexane
Man11anese
Mercury
Napthalene
Nickel
ll'UM
Toluene
Dryers
ODTWafers
Pollutanta
3-Garene
Cis-1,2-dichloroethytem
Cumene
Methyt ethyl ketone
Methyt isobutvl ketone
m,p.Xytene
Toluene
Spreadsheet Emissions
97
Nallll'all.tU
(lbelyr)
:>.Olt+v,
1.16E-04
1.06E-01
1.35E-01
1.16E-01
1.74E+02
3.68E-02
2.52E-02
5.90E-02
2.03E-01
6.39E-02
3.29E-01
356 270
OOT
(lb/vr)
2351.38
78.38
1959.48
317.08
277.89
356.27
534.40
1,337 HP Diesel-Emergency Generator
Hours of operation 11.1
nnlutant ·---· ~v2 3.00E-02
l/'IC8"'""'"Y"e L.00c-u.>
Acroleln 8.21E-04
Benzene 8.10E-02
Benzo(alovrene 2.66E-05
Formaldehyde 8.21E-03
Naphthalene 1.33E-02
PAH 2.22E-02
Propylene 2.89E-01
Toluene 2.89E-02
Xylene 2.00E-02
Bark Handling Fugitives
H f . 7 830.87 ours o operation
POiiutant
PM
PM10
TechShield
Gallons of Glue
Pollutant
IAC8taldehvae
Formaldehyde
Methanol
Vimn Acetate
ton .. yr
2.23
0.78
178 200
Emission Factor
(11191JT}
89.5883
267.1931
133.5965
1378.4019
Note: VOC, PM, PM-10 emissions based on AP--42 Table 1.6-3 Factors for Speciated Organic Compounds from
Wood Residue Combustion subtracted from the emissions generated from rates found in AP42 Table 10.6.1-3
Emission Factors for Dryers. These emissions are accounted for in the bark burner wood combustion section and
are based off manufactures' data.
Press 275 hp Diesel Fire Pump
MSF 3/8" basis 510 716 Hours of operation 21.8
Factor nn,utant ·---Pollutant llb/llSF ;n-1 PM " 1.32t+01
1,2,4-Trichlorobenzene 388.1441 PM10 1.32E+01
Bromomethane 204.2864 PM2.5 • 1.32E+01
cis-1 2-dichloroeth~lene 209.3935 NOX 1.86E+02
Cumene 5107.1597 co 4.00E+01
Methyt ethyt ketone 561.7876 SOX 7.27E+00
Methv1 1sobuM ketone 510.7160 voe 1.51E+01
Methylene Chloride 183.85n Acetaldehyde 3.22E-02
o-Xvlene 224.7150 Acroleln 3.88E-03
Stvrene 224.7150 Arsenic (H,T) 1.68E-04
Toluene 199.1792 Benzene 3.92E-02
BenzO{aJovrene 7.89E--06
Berv,lium (H' I J 1.26E-04
Cadmium (H,T) 1.26E-04
Chromium (H,T) 1.26E-04
Formaldehyde 4.95E-02
Lead IH) 3.78E-04
Manganese (H,T) 2.52E-04
Mercury (H,T) 1.26E-04
Naphthalene 3.56E-03
Nickel (H, T) 1.26E-04
Selenium (H) 6.29E-04
PAH 7.0501200E-03
Toluene 1.72E-02
XYiene 1.20E-02
Facility ID: 7300061 Permit No. 07760T24
Spreadsheet EMF
Louisiana Pacific Roxboro's Air Emissions Inventory
Other Emission Factors
Bark BumerfTOH's
Estimated Control Efficiency
HAPfTAP Pollutant Note WESP I RTu
-taldehvde Stack Test Data Used.
llc•to,,h•non• 5 0'M, I 90%
Arm!Ain Stack Test Data Used.
llnUmony 6 I 60'M, I 0'M,
Arsenic Stack Test Data Used.
Benzaldehyde , 0'4 I 90%
Benzene Stack Test Data Used.
Benzo(&IOIII'-57 80% 0'M,
B""'lhum 6 80% 0'M,
Bls-12-ethvlhexvll chlhlata , 0% 0%
Bromomelhane 5 0% 90%
Cadmium 6 60% 0%
Cwbon T etrac:hloride 5 0% 90%
Chlorine 5 0% 90%
Chlorobenz-5 0% 90%
Chloroform 5 0% 90%
Chloromethan• 5 0% 90%
Chromi'-'ll acid Nil 6 60'M, 0%
Clvomi'-"' 6 80% 0%
Coban 6 60'M, 0'M,
0/chloro,,.nz•n• , 0% 95%
1 2-0lchloro•th•n• 5 0% 90%
0/chlorom•lh•n• 5 0% 90%
1 2-0ich,omol'Dlllln• 5 0% 90%
4 f.Dln/tJo-2-m~,,,on.,,ol , 0% 90%
2 4-0initroohenol 5 0% 90%
2 4-0/nltrotolu•n• 1 0% 90%
Ethyl ,,.nan• 5 0% 90%
Fonnaldeh-Stack Test Data Used.
Huach/orol>Man• 5 I 0% I 90%
HlfCOD-TotaJ• 1,,,,,,.. -•-1 I 0% I 0%
HVdmnen Chloride 1 0% I 0%
LNd • tun/II lb/ton fuel) Stack Test Data Used.
MAnnanese Stack Test Data Used.
Mercuv· cuno -lb/ton fuel) 67 I 60'M, I 0%
Meth-.1 eth-.1 ketone 5 I 0% I 90%
Naothalene 58 0% I 90%
Nickel Stack Test Data Used.
4-Nilrophenol 5 0'4 I 90%
PentachlorOOll8llOI 5 0% I 90%
Phenol Stack Test Data Used.
Polvcnlorinaled bollllenVIS" 1 0% 0%
PCM 1 60% 95%
Selenium 67 60% 0%
Stvrene· 0% 90%
TCDD-2378• !<rill_..,..,.. 1 80% ()'JI,
T etrachlorelhene 5 0% 90%
Toluene , 8 0% 90%
Trlchlorobenzen• 1 0% 90%
1 1 1-Trichloroethane 1 0% 90%
Trichloroetheoe 1 0% 90%
2 •s.r· 1 0% 90%
VonV! chloride 5 0'M, 90%
Xvlene 5 0% 90%
Noles Conll<>IE
WESP RTO
2 0% 0%
Notes Control E
WESP RTO
2 3 0% 0%
Basis for Emission Rates:
3.04E-05
Woodwaste Combustion Controlled Woodwaste
Factor llblmmBTUl Combustion Factor
3.20E-09 I 3 20E-10
7.90E-06 I 1 58E-06
5.68E-05 I 5.68E-06
2.60E-06 5.20E-07
1.10E-06 2.20E-07
4.70E-08 4.70E-08
1.SOE-05 1.SOE-06
4.10E-06 8.20E-07
4.SOE-05 4.SOE-06
7.90E-04 7.90E-05
3.30E-05 3.30E-06
2.80E-05 2.60E-06
2.30E-05 2.30E-06
3.SOE-06 7.00E-07
2.10E-05 4.20E-06
650E-06 130E-06
3 37E-07 , 69E-06
2.00E-05 2.00E-06
2 90E-04 2.00E-05
330E-05 3.30E-06
2 10E-06 2.10E-07
, l!OE-07 1.60E-06
9.42E-07 9.42E-06
3.10E-05 310E-06
4 40E-03 I 440E-04
200E-09 I 2 OOE-09
3.40E-04 I 3.40E-04
3.SOE-06 I 7.00E-07
540E-06 I 540E-07
9 70E-05 I 9.70E-06
1.10E-07 I 1.10E-08
5.10E-06 I 5.10E-09
8.15E-09 1.20E-09
3.73E-05 3.73E-07
2.60E-06 560E-07
1.90E-03 1.SOE-04
8.60E-12 1.72E-12
3.60E-05 380E-06
9.20E-04 9.20E-05
3 21E-07 3 21E-06
3.10E-05 3.10E-06
3.00E-05 3.00E-06
2.20E-06 2.20E-09
1.80E-05 1.60E-06
2.SOE-05 2.SOE-06
Wood Cofflbu1bon Controlled
lbsJMMBtu ibsJMMB1u
0.01 1.00E-02
Wood Combustion we Controlled
lbslMMBlu lbs/MMBlu
0 2.SOE-02
11 Stack data was not available for the above HAPsfTAPa so the DAO Wood Waste Cornbusbon Emissions Calculator Spreadsheet wa, used to develop lls emission rate
baed on actual wood combultion
21 Batt< &mer emiSSIOO factors obtained from equipment manufacture tlYough Mid South Erlj,,-mg
3/ Emission Factors from AP-42 (9/2003), Tebla 1 6-1
Per Mid-South Engineering data, PM and TSP emissions based upon 2.5114 DB ash content In fuel. Mod-South data ind1catet that
emission, lit the bar1< b<.mer ex,1 we 1.7 lb PMIMMBtu. Mer exiting the pnmaiy cyclone, Blll1< Burner PM emiuions ate 0.3 lb/MMBtu
5/ AP-42 (9/2003). Table 1 6-3 Speaated Organic Compounds from Wood RHJdue CombuatJon
8/ AP-42 (9/2003). Table 1 6-4 Trace Elements from Wood Readle Cornbuttion
7/ AP-42 (7198) Table 1.4-4, Emiu,on Factors for Melals from natu-al gas ccmbustJon
8/ AP-42 (7/96) Table 1.4-3, Em,ssion Factors for speciated organic compounds from natural gas combustion
91 MACT stack testing conducted 8/30/06
• • Emission RatH laken from NCASI testing for panel plants
+ • Em!ss,on rat• taken from AP-42 chap4er 10 -OSB rn.-uectu-w,g
•·Emission ratH taken from NCASI testing for panel plants• 9ffllSSIOO factor Is 9 9€-7 i,wnlllon fuel for ell dooxins
LP Roxboro Facility ID· 7300061 Perm~ No. 07760T24
Spreadsheet EMF
Louisiana Pacific Roxboro's Air Emissions Inventory
Other TAP/HAP Emission Factors
RTO's/TOH's-aas
Nal Gas Combustion
Pollutant lb/mmscf
NOx 100
co 84
PM10 7.6
TSP 7.6
"'2 0.6
voe 5.5
Benzene* 2.10E-03
Benzo/alovrene• 1.20E-06
Cadmium" 1.10E-03
Chromium"" 1.40E-03
Cobalt• 8.40E-04
Dichlorobenzene• 1.20E-03
Formaldehvde• 7.SOE-02
Hexane• 1.80E+OO
Manaanese• 3.BOE--04
Mercury• 2.60E-04
Naothalene• 6.10E-04
Nickel• 2.10E-03
POM• 6.60E-04
Selenium" 2.40E-05
Toluene• 3.40E-03
Cobalt• 3.40E-03
l\t"-41.£ c1,~1 Table 1.4-4t, 1:.mIssIon t-actors tor Metals
from natural gas combustion.
• AP-42 (7/96) Table 1.4-3, Emission Factors for speciated
organic compooods from natural gas combustion
Drvers
Pollutant Note
3-<:arene 1
Acetaldehvde 1
Acrolein 1
Benzene 1
Cis-1 2-<lichloroethvlene 1
Cumene 1
Formaldehvde 1
Methanol 1
Methv1 ethvl ketone 1
Methvl isobuM ketone 1
m.o-Xvlene 1
Phenol 1
Prooionaldehvde 1
Toluene 1
WESP
0%
0%
0%
0%
0%
0%
0%
0%
0%
0%
0%
0%
0%
0%
' 7 1ese -Ire meraencv 1 33 HP o· If" d E G rator ene
Pollutant libs/hr\
PM 0.93
PM-10 0.93
PM-2.5 0.93
NOx 32
TOC, total 0.94 1:su, 5.4
co 7.3
11.~taldehvde 2.40E-04
Acrolein 7.40E-05
Benzene 7.30E-03
Benzol a \nurene 2 40E-06
Formaldehvde 7.40E-04
Naohthalene 1.20E-03
PAH 2.00E--03
Proovlene 2.60E-02
Toluene 2.60E-03
Xvtene 0.0018
Pollutants ,n red are federally regulated hazardous air pollutants (HAPs) only.
Pollutants in purple are NC regulated toxic air pollutants (TAPS) only.
All other pollutants are both HAPs and TAPs.
Bark Handlina Fuc itives
Pollutant lb/hr
PM 0.57
PM10 0.2
Control Efficlencv Emission Factor I Controlled Combustion
RTO (lb/ODT) Factor llb/ODTI
90% 0.066 I 6.60E-03
90% Stack Test Data Used
90% Stack Test Data Used
90% Stack Test Dala Used
90% 0.0022 I 2.20E-04
90% 0.055 I 5.SOE--03
90% Stack Test Data Used
90% Stack Test Data Used
90% 0.0089 I 8.90E-04
90% 0.0078 I 7.80E-04
90% 0.01 I 1.00E-03
90% Stack Test Data Used
90% 0.011 I 1.10E-03
90% 0.015 I 1.SOE--03
1/ AP-42 (3/2002), Table 10.6.1-3, Rotary Dryer, direct wood-fired, softwood (uncontrolled)
LP Roxboro Facility ID: 7300061 Permit No. 07760T24
Spreadsheet EMF
Louisiana Pacific Roxboro's Air Emissions Inventory
Other TAP/HAP Emission Factors
D ,rvers Th erma IO"IH I eate rs a n dD 1rver RTO' 4-6 s
1.SOE->-01
HAP/TAP &ti1Mted Control EfficlenCY Woodwast• Combustion Woodwaate Combustion Factor (lblnvnBtul
(lbllhr) WESP RTO Fador (tblmmBTU) WESP + RTO Control WESP ♦ RTO Contror
"vi v,. U7" 2.'IVC-V~ 2.40c-v~ 2.40E-02
Acetoohenon• 0% 90% 3.23E-09 3.23E-10 3.23E-10
Wlt,monv 80% 0% 7 94E-06 1.59E-06 1 59E-06 -80% 0% 3.85E-06 7.70€-07 7.70E-07
Benzaldenvae 0% 90% 5.68E-05 5.68E-06 5.68E-06
Benzene 0% 90% Included w/Drver Emission, NA 0
Benzo(aJpyrena 80% NA
Barv1Iium 80% 0% 7.71E-07 1.54E-07 1.54E-07
8/a-(2-,,thy/he:,n,/I nhth/ale 0% °" 4.65E-08 4.SSE-08 4.SSE-08
Bromometh•n•+ 0% -BDL 0 0
Cadmi\.lll 80% 0% 2.87E-06 5.74E-07 5.74E-07
Carbon Tetrachloride 0% 90% 2.76E-05 2.76E-06 2.76E-06
ChlOfine 0% 0% 6.01E-04 6.01E-04 6.01E-04
Chlorobenzene 0'Mt 90% 1.66E-05 1.66E-06 1.66E-06
Chlorofonm 0% 90% 2.70E-05 2.70E-06 2.70E-06
Chlororru,thane 0% -2 31E-05 2.31E-06 2.31E-06
Cobalt 80% 0% 6 57E-06 1.31E-06 1 31E-06
D1Chlorobenzene 0% 90% 3.37E-07 3.37E-08 3.37E-08
1 2•Dlch/oroeth•ne+ 0% 90" BDL 0 0
D/chlororrHkthane 0% 90" 294E-04 2.94E-05 2 94E-05
1 2•D/ch/oroon,oane 0% -3 33E-05 3.33E-06 3 33E-06
4.S-Dinltro-2-tMth"'"h•nol 0% -210E-06 2 10E-07 210E-07
2 4-Dlnitrophenol 0% -4.78E-07 4.78E-08 4.78E-08
2 4-Dlnltrotolu•n• 0% 90" 9.42E-07 9.42E-08 9.42E-08
Ettw1benzene 0% -3.13E-05 3.13E-06 313E-06
Hex•chloroNnzen•• 0% -1.20E-07 1.20E-08 1.20E-08
He.-0% 90% O.OOE+OO 0 0
HxCDD-T otat• tun/tf • amSllt>n fuoll 0'Mt °" 2.00E-09 2.00E-09 2.00E-09
Hvdroaen Chloride" 0% 0% 3.40E-04 3.40E-04 3.40E-04
Lead • rooits lb/Ion fuell 80% 0% 240E-03 4.SOE-04 4.80E-04
Manoanese 80% 0% 1.12E-03 2.24E-04 2.24E-04
Me<curv· ru,.ta -lb/Ion fuell 80% 0% 5.SOE-10 1.18E-10 1.18E-10
Methvl eu,yl ketone· 0% 90'Mt ND 0 0
Naothalene 0% 90% 1.32E-04 1.32E-05 1.32E-05
Nickel 80'4 0% 2.31E-05 4.62E-06 4.62E-06
4-Nitr~enol 0% 90% 3.31E-07 3.31E-08 3.31E-08
Pentachloroor-,oi 0% 90% 237E-07 2.37E-08 2.37E-08
Phenol" 0% 90% Included w,1 __.. Emission! 0 0
Polvchlorinated biDnenv,s• 0% 0% ND 0 0
POM 80% 95% 3.73E-05 3.73E-07 3.73E-07
Selenium 80% 0% 5.43E-06 1.0SE-06 1 OSE-06
Smwne" 0% 90% ND 0 0 7~2378• ___ ..., 90% °" 2.00E-09 200E-10 200E-10
r etrachlorethene O'Mt 90% 389E-05 389E-06 3.89E-06
Toluene 0% 90% Included w/Drver Emission, 0 0
Triehlorobenzene 0% 90% 3.21E-07 3.21E-08 3.21E-08
1 11-Trichloroelhane 0'Mt 90% 3.23E-05 3.23E-06 3.23E-06
T riehloroelhene 0% 90% 3.19E-05 3.19E-06 3.19£-06
2.46-Trieh-0% 90% 2 18E-07 2.18E-08 2.18E-08
Vinv1 chloride 0'Mt 90% 1.31E-05 1.31E-06 1.31E-06
Xvlene 0% 90% ND 0 0
Stack data was nol ■va,lable for the above HAPa/TAPs DAQ'a Wood Waste Combustion Emlaaions Calculator Spreadsheet was used to develop ,ts emlaaion rate based on
8Clu■l wood combua1Jon
A 90% destruction effic,ency for organics In add,bOn. nat,..., gas combusbOn em,uoons from RTOs were -to total
A 90% oontrol elf,caency for lnorganics was Haumed for the WESPa Statck test data perfonmed ,n Jan 05 indicated WESP PM oontrol elf,c,ency of 91 79'Mt
• -Emission Ratea taken from NCASI testing for panel plants
+ • Emission rates taken from AP-42 chapter 10 • OSB manufacturing
• • Emission rate, 18ken from NCASI testJng tor panel planta -emIssIon factor 11 9 9E-7 grama/ton fuel for all dioxins
Press
E1tl1Mted Control Efficiency Emission Factor Controlled Emlaalon Facto,
Pollutant Note .. ,v "~•~r ~n "=-~r ~n
1 2 4-T richlorobenzene 4 90% 00076 0.0008
1 2-diehloroethane 4 90% 0.0041 0.0004
Acetone 4 90% 0.0027 0.0003
Bromomethane 4 90% 0.004 0.0004
Chloroethane 4 90% 0.0027 0.0003
ChloroeU.-4 90% 0.0026 0.0003
cis-1 2-diehloroernvlene 4 90% 00041 0.0004
Cumene 4 90% 0.1 0.0100
Methvl ethvl ketone 4 90'Mt 0.011 0.0011
Methvl iso~ =I ketone 4 90% 0.01 0.0010
,-Chlonde 4 90% 00038 0.0004
o-Xvlene 4 90'Mt 0,()04,1 0.0004
Stvrene 4 90% 0.0044 0.0004
1oluene 4 90% 0.0039 0.0004
1/ Obtaned from NCASI stack test on panel plants. Emission factor ,s hsted ea reported by LP in (2002 El template.xfs)
In _.. ~. bolh NCASI ennsion data and AP-42 factors were av.-for the same pollutant In auCh Slluationa,
the NCASI stad< test data was ut1hzed since • was obl...-.d from stte-.peaf,c tests and Is more repra-.ve of faaloty emtssionS
~ Obtained from NCASI Tectv>ICel Bulle!Jn No 772 (MIi 410) Page 74, OSB Hot Prass and RTO Emossoona, RTO lnlel
Bulletin information was uHd over AP-42 emlaaion factora a1nce ~ is mora
7/ MDI emlsaiOn factor Is baHd on stack tasting .i other Loulala~acif,c OSB facilities Emission factor la listed as reported by LP in (2002 El Template xis)
LP Romoro Facility ID 7300061 Permit No. 07760124
Spreadsheet EMF
TechShield
Pollutant Note Emission Factor Ub/aall
"°8laldNW<1e 1 0.00050274
Formaldehvoe 1 0.00149940
Methanol 1 0.00074970
Vinvl Acetate 1 0.00773514
11 Obtained from vendor ema,I Information IIMet provided AO doong permitting of line
275 HP Diesel Fire Pum )
Pollutant (lblhp-hrl• 275HP
PM• 2.20E-03 06050
PM10 2.20E-03 06050
PM2.5 • 2.20E-03 0,6050
NOX 3.10E-02 8,5250 co 6.68E-03 1.8370
SOX 1.21E-03 0.3337
vvo., 2.51E-03 0.6914
Acelaldenya IH Tl 5.37E-06 0.0014765
Acrolein CH, 1 6.48E-07 0.0001781
Araenic(HT 2.80E-08 0.0000077
Benzene <H n 6.53E-06 0.0017960
Beru:O(alOllr8f18 IH.Tl 1.32E-09 0.0000004
B"""lnm (H,TI 2.10E-08 0.0000058
C9<lmkxn (H,T) 2.10E-08 0.0000058
Chromium IH Tl 2.10E-08 0.0000058
Formaldehyde (H Tl 8.26E-06 0.0022715
Lead rHl 6.30E-08 0.0000173
MAn<>anese H Tl ◄.20E-08 00000116
Marr•~rH, r1 2.10E-08 0.0000058
Naothalene Hl 5.9◄E-07 0.0001632
Nickel rH,T 2.10E-08 0.0000058
Selenium (Hl 1.0SE-07 0.0000289
Total PAH IHI 1.18E-06 0.0003234
Toluene IH.Tl 2.86E-06 0.0007873
Xvlene (H, Tl 2.00E-06 0.000:>'186
I• Emission factors from DENR Peovided spraedsheet for Internal Combustion (small gasoline and diesel engines)
LP Roxboro Faality ID 7300061 Permit No. 0TT60T24
LP Roxboro
Louisiana Pacific Roxboro's Air Emissions Inventory -Total Facility Emissions
!Tons/Yr Emissions I Total Facilitv
DryersfTOH/
Bark Burner
PM 68.09 29.90
PM-10 66.4 29.63
PM-2.5 66.4 29.63
so, 6.85 6.75
NOx 141.25 134.17
voe 129.91 28.52
co 116.33 110.69
kbs/Yr Emissions I Total Facilit-,
DryersfTOH/
Bark Burner
1, 1, 1-Trichloroethane 3.5799 3.5799
1,2-Dichloroethane 3.3489 3.3489
1,2-Dichloroorooane 3.8109 3.8109
2,4,6-Trichlorophenol 0.0025 0.0025
2,4-Dinitrophenol 0.0208 0.0208
2,4-Dinitrotoluene 0.1088 0.1088
4,6-Dinitro-2-methvtnhenol ( 0.2425 0.2425
4-Nitroohenol 0.0127 0.0127
Acetaldehyde 19923.7 18,715.78
Acetoohenone 0.00037 0.00037
Acrolein 6047.97 4,855.14
Antimonv 1.8246 1.8246
Arsenic 4.70 4.70
Benzene 264.88 234.94
Benzo(a)pyrene 0.6008 0.6006
Beryllium 0.254 0.2541
Bis-(2-ethylhexvl) phthlate (1 0.0543 0.0543
Bromomethane 206.02 1.73
Cadmium 1.1848 1.0782
Carbon Tetrachloride 5.1966 5.1966
Chlorine 91.2296 91.2296
Chlorobenzene 3.8109 3.8109
Chloroform 3.2335 3.2335
Chloromethane 2.6561 2.6561
Chromium (VI) 0.8084 0.8084
Chromium 13.998 13.862
Cobalt 1.6015 1.6015
Cumene 7066.64 1959.48
Dichlorobenzene 0.2788 0.1627
Dichloromethane 217.3471 33.4893
Ethyl benzene 3.5559 3.56
Formaldehyde 8696.93 3289.45
Hexachlorobenzene 508.11 508.11
Hexane 389.0160 214.8660
Hvdroaen Chloride 392.6335 392.6335
Lead 4.6989 4.6985
Manaanese 21.9659 21.9289
MDI 26.163 0
Mercurv 0.8647 0.8394
Methanol 57,255.45 3,288.97
Methvl ethyl ketone 317.14 317.14
Methyl isobutv1 ketone 788.61 277.89
Naohthlalene 11.35 11.2744
Nickel 21.1253 20.9220
Pentachloroohenol 0.0059 5.85E-03
Phenol 7942.74 1,879.431
Polvchlorinated biphenvls 0.0014 1.39E-03
POM 0.6026 0.5095
Proovlene 0.289 0
Propionaldehvde 5,969.65 4,776.83
Selenium 0.650 0.650
Stvrene 444.128 219.4129
Tetrachlorethene 4.3883 4.39
Toluene 743.9490 544.3948
Trichlorobenzene 0.0371 3.71E-02
Trichloroethene 3.4644 3.4644
Vinyl Acetate 1378.4019 0
Vinvl Chloride 2.0786 2.0786
Xvlene 581.2773 356.5303
Pollutants in red are federally regulated HAPs only.
Pollutants in purple are NC regulated TAPs only.
All other pollutants are both HAPs and TAPs.
Press Bark Fug CP-003/004
(G-67) (F-1) CP-001 CP-002 (G-58)
20.45 2.23 4.40 2.16 2.20
20.45 0.78 4.40 2.16 2.20
20.45 0.78 4.40 2.16 2.20
0.06 0.00 0 0 0
6.82 0.00 0 0 0
4.65 0.00 9.09 51.06 9.09
5.58 0.00 0 0 0
Press Bark Fug CP-003/004
(G-67) (F-1) CP-001 CP-002 (G-58)
0 0 0 0 0
0 0 0 0 0
0 0 0 0 0
0 0 0 0 0
0 0 0 0 0
0 0 0 0 0
0 0 0 0 0
0 0 0 0 0
1,118.27 0 0 0 0
0 0 0 0 0
1192.82 0 0 0 0
0 0 0 0 0
0 0 0 0 0
29.82 0 0 0 0
0.00012 0 0 0 0
0 0 0 0 0
0 0 0 0 0
204.29 0 0 0 0
0.1064 0 0 0 0
0 0 0 0 0
0 0 0 0 0
0 0 0 0 0
0 0 0 0 0
0 0 0 0 0
0 0 0 0 0
0 135 0 0 0 0
0 0 0 0 0
5107.16 0 0 0 0
0.1161 0 0 0 0
183.8577 0 0 0 0
0 0 0 0 0
1301.06 0 0.00 3166.44 401 .11
0 0 0 0 0
174.1500 0 0 0 0
0 0 0 0 0
0 0 0 0 0
3.68E-02 0 0 0 0
4.995 0 0 20.874 0
0.0252 0 0 0 0
1,301.06 0 0 51,071.60 901 .04
0 0 0 0 0
510.72 0 0 0 0
0.0590 0 0 0 0
0.2032 0 0 0 0
0 0 0 0 0
5464.661 0 0 590.45 0
0 0 0 0 0
0.0639 0 0 0 0
0 0 0 0 0
1,192.82 0 0 0 0
0 0 0 0 0
224.72 0 0 0 0
0 0 0 0 0
199.5082 0 0 0 0
0 0 0 0 0
0 0 0 0 0
0 0 0 0 0
0 0 0 0 0
224.7150 0 0 0 0
CP-005 TechShield MDI Tanks Emg Gen Fire Pump Edgeseal (IS Printing Op Misc.
(GRS) CP-006 CP-007 FUELPREP (GR1) (G-62) (ENG-1) (IS-DF-1) EO-1) (IS-PO-1) (G-74)
0.48 3.27 0.06 1.77 0 0 0.005 0.01 1.16 0 0
0.48 3.27 0.06 1.77 0 0 0.005 0.01 1.16 0 0
0.48 3.27 0.06 1.77 0 0 0.005 0.01 1.16 0 0
0 0 0 0 0 0 0.03 0.00 0 0 0
0 0 0 0 0 0 0.18 0.09 0 0 0
7.72 5.03 0.56 12.68 1.10 0.00 0.005 0.01 0.25 0.13 0.01
0 0 0 0 0 0 0.041 0.02 0 0 0
CP-005 TechShield MDI Tanks Emg Gen Fire Pump Edgeseal (IS Printing Op Misc.
(GRS) CP-006 CP-007 FUELPREP (GR1) (G-62) (ENG-1) (IS-DF-1) EO-1) (1S-PO-1) (G-74)
0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0 0 0
0 0 0 0 89.59 0 0.0027 0.0322 0 0 0
0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0.0008 0.0039 0 0 0
0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0.00017 0 0 0
0 0 0 0 0 0 8.10E-02 0.03915 0 0 0
0 0 0 0 0 0 0.0000 0.0000 0 0 0
0 0 0 0 0 0 0 0.0001 0 0 0
0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0.0001 0 0 0
0 0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0.00 0 0 0
0 0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0 0 0 0
214.50 0.00 0.00 57.12 267.19 0.00 0.01 0.05 0.00 0.00 0.00
0 0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0.0004 0 0 0
0 0 0 0 0 0 0 0.0003 0 0 0
0.276 0 0 0 0 0.0178 0 0 0 0
0 0 0 0 0 0 0.0000 0.0001 0 0 0
0 0 279.59 279.59 133.59654 0 0 0 0 0 0
0 0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0.0133 0.00356 0 0 0
0 0 0 0 0 0 0.0000 0.0001 0 0 0
0 0 0 0 0 0 0 0 0 0 0
8.20 0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0.0222 0.0071 0 0 0
0 0 0 0 0 0 2.89E-01 0 0 0
0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0.001 0 0 0
0 0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0.0289 0.0172 0 0 0
0 0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0 0 0 0
0 0 0 0 1,378.4019 0 0 0 0 0 0
0 0 0 0 0 0 0 0 0 0 0
0 0 0 0 0.00 0 0.0200 0.01196 0 0 0
Permit No. 07760T24
Facility ID: 7300061