AQ_F_6600016_20221115_EI_Cmb-EI-File_2021 EI

2021 Emissions Inventory Review / Data Tracking Form
Facility Name: Bakelite Chemicals LLC - Conway
Facility
Classification:
Title V

Assigned to:
Dawn Reddix

Data Entry:

Northampton County
Confidential Copy Submitted?
 YES
 NO
 Enter date received into ED. Date Received: _________________
 Assigned to appropriate individual. Date Assigned: _________________ Date Due: __________________
 Paper copy submitted: One copy received with supporting documentation, certification form signed by responsible
official, and appears generally complete; OR
 Electronic copy submitted: All supporting documentation and certification form (with time/date stamp) signed by
responsible official has been received.
Comments:
Facility ID: 6600016
Initial Review / Data Entry
Inventory Review
 All forms and supporting documentation appear to be complete if paper submission (check ED OS data if electronic).
 Contact, address, phone number changes entered into I-Beam/Facilities if necessary.
 All known operating scenarios, control devices, and emission release points have been entered for each emission
source (permitted, insignificant, and unpermitted) or note that the emission source was not operated or not required to report.
 Check if SCC codes for each OS are accurate and update if needed.
 Evaluate "U" sources for significance and address according to policy.
 Calculations / forms appear to add up correctly.
 All compliance issues are being addressed (e.g. Toxics limits, above TV thresholds, large emissions
increase/decrease, installation without a permit).
 All volatile HAPs/TAPs were included in the VOC total.
 Calculations and control efficiencies appear correct. Emission factors are the best available and most current factors
appropriate for the reporting facility (e.g. stack testing, AP-42, etc.).
 Review facility comments and address any issues.
 Update ED (Data Entry Main) if additional information is required (corrections due date and date received).
 Check all ED QA/QC reports.
 Comparison with previous emission inventory must be made and outliers (> 10%) must be investigated and explained.
 Put inventory review comments and summarize any changes in ED - Data Entry Main "DAQ internal comments".
Date Review Complete: ___________________ Signature: _____________________________
Date Submitted to EI Coordinator: ___________________
Date Approved: ___________________ Initials: ___________________
Date Info Requested: ______________ Date Info Received: ______________ Total Days on Hold: ______
Alan Drake/Jeff Harris
11/10/2022
Changes due to apparent throughput increase, but also significant changes to calculation methodology.
See notes.
11/15/2022
COPY of RECORD Date Submitted: 5/20/2022 08:34:49
Inventory Certification Form(Title V) Facility Name: Georgia-Pacific Chemicals LLC -Conway
200 Ampac Road
Conway, NC 27820
North Carolina Department of Environmental Quality
Division of Air Quality
Facility ID : 6600016Permit : 04243 County : Northampton
DAQ Region : RRO
Air Pollutant Point Source Emissions Inventory -Calendar Year 2021
These forms must be completed and returned even if the facility did not operate or emissions were zero
The legally defined "Responsible Official ti of record for your facility is Robert Dalton
This person or one that meets the definition below must sign this certification form.
The official submitting the information must certify that he/she complies with the requirements as specified in Title 15A NCAC
2Q.0520(b) which references and follows the federal definition. 40 CFR Part 70.2 defines a responsible as meaning one of the
following:
1.For a corporation: a president, secretary, treasurer, or vice-president of the corporation in charge of a principal business
function, or any other person who performs similar policy or decision making functions for the overall operation of one or
more manufacturing, production, or operating facilities applying for a or subject to a permit and either
i.the facilities employ more than 250 persons or have gross annual sales or expenditures exceeding $25 million(in
second quarter 1980 dollars); or
ii.the delegation of authority to such representatives is approved in advance by the permitting authority;
2.For partnership or sole 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 of a principal geographic unit of the agency (e.g., a Regional Administrator of EPA).
CERTIFICATION STATEMENT:
(lm�ortant: Le2all)'. Resuonsible Official, read and sii:n after all submissions are final.)
I certify that I am the responsible official for this facility, as described above, and hereby certify that the information contained in
this air emissions report, including attached calculations and documentation, is true, accurate and complete. (Subject to legal
penalties of up to $25,000 per occurrence and possible imprisonment as outlined in G.S. § 143-2 l 5.3(a)(2))
Responsible Official's Signature Below (use blue ink): Date Signed:
Printed Name: Robert Dalton 5lzo\ 2 2 Signature: K [. �
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.
Email address of Responsible Official: [e-mail]
Information on this Form cannot be held confidential
COPY of RECORD Date Submitted: 5/2012022 08:34:49 .tal QuaUt)'NC Dept of Env1ronmen
MAY 2 3 2022
Raleigh Regional Office
Bakelite Chemicals LLC - Conway 04243T27
6600016
Facility Name:
Facility ID #:
Permit #(s):
Facility Total CY 2021 Emission Summary Recorded in ED
Pollutant CAS CY 2021
from ED
CY 2020
from Fees
Green House Gases Pollutants (GHG)Actual Emissions
Tons/Yr %
ChangeDemini-
mus
Carbon Dioxide (CO2)124389 12,226.43 10,839.12 12.8%5,000.0
Methane (CH4)74-82-8 0.180000 0.180000 0.0%10.0
Nitrous Oxide (N2O)10024972 0.014800 0.010000 48.0%1.0
CO2 equivalent (sum of individual GHG pollutant emission
times their 1995 IPCC Global Warming Potential (GWP),
converted to metric tons)
11,099.41 metric tons
Criteria Pollutants
CY 2021
from ED
CY 2020
from Fees
(Tons/Year)
Actual Emissions
%
ChangePollutantCASDemini-
mus
-29.9%30.0421.07CO 0.5CO
0.0%7.987.98NOx 0.5NOx
1.2%32.9033.30TSP 0.5PM(TSP)
1.7%26.2326.67PM10 0.5PM10
1.7%24.9525.37PM2.5 0.5PM2.5
40.0%0.0500000.070000SO2 0.5SO2
12.7%85.0695.84VOC 0.5VOC
Hazardous Air Pollutants (HAPs)
and/or Toxic Air Pollutants (TAPs)
CY 2021
from ED
CY 2020
from Fees
(Pounds/Year)
Actual Emissions
%
ChangePollutantCASDemini-
mus
Polycyclic Organic Matter (Specific Compounds from OAQPS
for TV)
0.003850 0.004940 N/A1.0
N/A0.0049400.00385091-20-3 1.0Naphthalene (Component of 83329/POMTV)
3.1%238.70246.1375-07-0 10.0Acetaldehyde
N/A0.0003000.000230107-02-8 10.0Acrolein
3.0%616.66635.437664-41-7 100.0Ammonia (as NH3)
5.3%0.3965300.41772071-43-2 1.0Benzene
3.2%935.90966.101319-77-3 10.0Cresol (mixed isomers)
Page 1 of 211/09/2022
Bakelite Chemicals LLC - Conway 04243T27
6600016
Facility Name:
Facility ID #:
Permit #(s):
Facility Total CY 2021 Emission Summary Recorded in ED
Hazardous Air Pollutants (HAPs)
and/or Toxic Air Pollutants (TAPs)
CY 2021
from ED
CY 2020
from Fees
(Pounds/Year)
Actual Emissions
%
ChangePollutantCASDemini-
mus
4.3%11,776.3512,287.2350-00-0 10.0Formaldehyde
13.2%304.89345.26110-54-3 100.0Hexane, n-
-0.4%196.11195.3378-93-3 100.0MEK (methyl ethyl ketone, 2-butanone)
5.2%101,746.08107,003.2967-56-1 1,000.0Methanol (methyl alcohol)
2.1%3,106.813,171.19108-95-2 100.0Phenol
-22.0%0.0080600.006290POM 1.0Polycyclic Organic Matter (Inc PAH, dioxins, etc. NC
& AP 42 historic)
2.7%484.00497.00100-42-5 100.0Styrene
12.6%0.5868100.660780108-88-3 100.0Toluene
N/ANot
Reported
542.00121-44-8 100.0Triethylamine
-22.1%0.0073400.0057201330-20-7 100.0Xylene (mixed isomers)
Largest Individual HAP 107,003.29 lbs
125,059.29 lbsTotal HAP Emissions
Methanol (methyl alcohol)
Largest Individual CAP 95.84 tons
Total CAP Emissions 151.63 tons
Total TAP Emissions 18,344.75 lbs
Total Aggregate
Emissions
151.95 tons
VOC
Page 2 of 211/09/2022
DAQ's Comments Regarding Inventory
CO decrease linked to OS1 Formaldehyde Mfg, despite apparent increase in production relative to
2020.
VOC increase primarily results from cited production increase for OS1 Formaldehyde Mfg relative to
2020.
n-Hexane increase linked to increased NG combustion for OS21 resin mfg thermal oxidizer and OS55
spray dryer.
Facility added the following: emission differences between 2020RY and 2021RY are due to a change in
the calculation methodology and a broken link within the AEI spreadsheet between the two years.
While working through the 2021RY report, we realized that the in previous years, the OS1
calculations were based on 100% formaldehyde concentration but should have been based on 50%
formaldehyde concentration. Once we changed the gallons to represent the throughput at 50%
concentration and properly linked the CO to the 2016 Stack Test value for CO, it gave the appearance
that the 2021RY throughput increased while the CO decreased. In summary, it appears that we
underreported the CO emissions for the 2020RY. We are comfortable saying that the 2021RY
emission values and associated calculations are now correct and that methodology will be transferred
to future submissions.
Facility Emissions - Operating Scenarios Per Pollutant
Bakelite Chemicals LLC - Conway
2021 Inventory
Bakelite Chemicals LLC - Conway
6600016 04243T27
Facility Name:
Facility ID:Permit Number(s):
Emission Rate - 2021OS ID Emission
Source ID
Pollutant
Emission Rate (Prev) - 2020
Acetaldehyde
OS-1 20.13 Pounds 18.70 Pounds
VS2A-ES-2 VS2A-ES-2
OS-27 0.000750 Pounds 0.000960 Pounds
ES-GEN1 ES-GEN1
ES-GEN2 ES-GEN2
OS-54 226.00 Pounds 220.00 Pounds
VS5A VS5A
TOTAL in Current Inventory: 246.13 Pounds TOTAL in Previous Inventory: 238.70 Pounds
Acrolein
OS-27 0.000230 Pounds 0.000300 Pounds
ES-GEN1 ES-GEN1
ES-GEN2 ES-GEN2
TOTAL in Current Inventory: 0.00 Pounds TOTAL in Previous Inventory: 0.00 Pounds
Ammonia (as NH3)
OS-12 36.77 Pounds 26.88 Pounds
VS4A.1-ES4.1 VS4A.1-ES4.1
OS-40 278.66 Pounds 272.78 Pounds
ES-S19 ES-S19
OS-54 320.00 Pounds 317.00 Pounds
VS5A VS5A
TOTAL in Current Inventory: 635.43 Pounds TOTAL in Previous Inventory: 616.66 Pounds
Benzene
OS-3 0.037900 Pounds 0.036900 Pounds
ES-B1 ES-B1
11/9/2022 Page 1 of 13
Bakelite Chemicals LLC - Conway
6600016 04243T27
Facility Name:
Facility ID:Permit Number(s):
Emission Rate - 2021OS ID Emission
Source ID
Pollutant
Emission Rate (Prev) - 2020
OS-20 0.050000 Pounds 0.060000 Pounds
VS2A-ES-2 VS2A-ES-2
OS-21 0.050000 Pounds 0.030000 Pounds
VS4A.1-ES4.1 VS4A.1-ES4.1
OS-27 0.023000 Pounds 0.029500 Pounds
ES-GEN1 ES-GEN1
ES-GEN2 ES-GEN2
OS-33 0.000010 Pounds
I-HTF I-HTF
OS-37 0.006810 Pounds 0.010130 Pounds
ES-B2 ES-B2
OS-55 0.250000 Pounds 0.230000 Pounds
VS5A VS5A
TOTAL in Current Inventory: 0.42 Pounds TOTAL in Previous Inventory: 0.40 Pounds
Carbon Dioxide (CO2)
OS-3 1,076.93 Tons 1,048.39 Tons
ES-B1 ES-B1
OS-20 2,290.78 Tons 2,298.32 Tons
VS2A-ES-2 VS2A-ES-2
OS-21 1,503.43 Tons 787.73 Tons
VS4A.1-ES4.1 VS4A.1-ES4.1
OS-27 3.10 Tons
ES-GEN1
ES-GEN2
OS-33 0.400000 Tons 0.400000 Tons
I-HTF I-HTF
OS-37 193.00 Tons 288.00 Tons
ES-B2 ES-B2
OS-55 7,161.89 Tons 6,413.18 Tons
VS5A VS5A
TOTAL in Current Inventory: 12,226.43 Tons TOTAL in Previous Inventory: 10,839.12 Tons
11/9/2022 Page 2 of 13
Bakelite Chemicals LLC - Conway
6600016 04243T27
Facility Name:
Facility ID:Permit Number(s):
Emission Rate - 2021OS ID Emission
Source ID
Pollutant
Emission Rate (Prev) - 2020
CO
OS-1 4.57 Tons 13.81 Tons
VS2A-ES-2 VS2A-ES-2
OS-2 4.18 Tons 4.19 Tons
VS4A.1-ES4.1 VS4A.1-ES4.1
OS-3 0.760000 Tons 0.740000 Tons
ES-B1 ES-B1
OS-27 0.010000 Tons 0.010000 Tons
ES-GEN1 ES-GEN1
ES-GEN2 ES-GEN2
OS-37 0.140000 Tons 0.200000 Tons
ES-B2 ES-B2
OS-54 11.41 Tons 11.09 Tons
VS5A VS5A
TOTAL in Current Inventory: 21.07 Tons TOTAL in Previous Inventory: 30.04 Tons
Cresol (mixed isomers)
OS-12 108.10 Pounds 99.90 Pounds
VS4A.1-ES4.1 VS4A.1-ES4.1
OS-54 858.00 Pounds 836.00 Pounds
VS5A VS5A
TOTAL in Current Inventory: 966.10 Pounds TOTAL in Previous Inventory: 935.90 Pounds
Formaldehyde
OS-1 3,037.89 Pounds 2,821.25 Pounds
VS2A-ES-2 VS2A-ES-2
OS-2 22.29 Pounds 21.72 Pounds
VS4A.1-ES4.1 VS4A.1-ES4.1
OS-3 1.35 Pounds 1.32 Pounds
ES-B1 ES-B1
OS-10 150.00 Pounds 110.00 Pounds
VS2A-ES-2 VS2A-ES-2
OS-12 534.10 Pounds 510.40 Pounds
11/9/2022 Page 3 of 13
Bakelite Chemicals LLC - Conway
6600016 04243T27
Facility Name:
Facility ID:Permit Number(s):
Emission Rate - 2021OS ID Emission
Source ID
Pollutant
Emission Rate (Prev) - 2020
VS4A.1-ES4.1 VS4A.1-ES4.1
OS-19 15.01 Pounds 14.97 Pounds
PFTF PFTF
OS-27 0.002340 Pounds 0.003000 Pounds
ES-GEN1 ES-GEN1
ES-GEN2 ES-GEN2
OS-29 36.84 Pounds 33.84 Pounds
ESR8 ESR8
UFTF UFTF
OS-33 0.000500 Pounds
I-HTF I-HTF
OS-37 0.243220 Pounds 0.361930 Pounds
ES-B2 ES-B2
OS-41 1.50 Pounds 1.49 Pounds
I-P11 I-P11
I-P12 I-P12
OS-54 8,488.00 Pounds 8,261.00 Pounds
VS5A VS5A
TOTAL in Current Inventory: 12,287.23 Pounds TOTAL in Previous Inventory: 11,776.35 Pounds
Hexane, n-
OS-3 32.49 Pounds 31.63 Pounds
ES-B1 ES-B1
OS-20 46.79 Pounds 48.61 Pounds
VS2A-ES-2 VS2A-ES-2
OS-21 44.05 Pounds 22.46 Pounds
VS4A.1-ES4.1 VS4A.1-ES4.1
OS-33 0.010000 Pounds 0.010000 Pounds
I-HTF I-HTF
OS-37 5.84 Pounds 8.69 Pounds
ES-B2 ES-B2
OS-55 216.08 Pounds 193.49 Pounds
VS5A VS5A
11/9/2022 Page 4 of 13
Bakelite Chemicals LLC - Conway
6600016 04243T27
Facility Name:
Facility ID:Permit Number(s):
Emission Rate - 2021OS ID Emission
Source ID
Pollutant
Emission Rate (Prev) - 2020
TOTAL in Current Inventory: 345.26 Pounds TOTAL in Previous Inventory: 304.89 Pounds
MEK (methyl ethyl ketone, 2-butanone)
OS-12 194.59 Pounds 195.42 Pounds
VS4A.1-ES4.1 VS4A.1-ES4.1
OS-44 0.740000 Pounds 0.690000 Pounds
I-A2 I-A2
TOTAL in Current Inventory: 195.33 Pounds TOTAL in Previous Inventory: 196.11 Pounds
Methane (CH4)
OS-3 0.020000 Tons 0.020000 Tons
ES-B1 ES-B1
OS-20 0.030000 Tons 0.030000 Tons
VS2A-ES-2 VS2A-ES-2
OS-21 0.010000 Tons
VS4A.1-ES4.1
OS-55 0.130000 Tons 0.120000 Tons
VS5A VS5A
TOTAL in Current Inventory: 0.18 Tons TOTAL in Previous Inventory: 0.18 Tons
Methanol (methyl alcohol)
OS-1 2,558.32 Pounds 2,375.89 Pounds
VS2A-ES-2 VS2A-ES-2
OS-2 228.49 Pounds 222.98 Pounds
VS4A.1-ES4.1 VS4A.1-ES4.1
OS-10 716.00 Pounds 415.00 Pounds
VS2A-ES-2 VS2A-ES-2
OS-12 3,790.30 Pounds 3,324.30 Pounds
VS4A.1-ES4.1 VS4A.1-ES4.1
OS-19 837.21 Pounds 829.66 Pounds
PFTF PFTF
OS-29 32.66 Pounds 29.99 Pounds
ESR8 ESR8
11/9/2022 Page 5 of 13
Bakelite Chemicals LLC - Conway
6600016 04243T27
Facility Name:
Facility ID:Permit Number(s):
Emission Rate - 2021OS ID Emission
Source ID
Pollutant
Emission Rate (Prev) - 2020
UFTF UFTF
OS-41 10.31 Pounds 10.26 Pounds
I-P11 I-P11
I-P12 I-P12
OS-54 98,830.00 Pounds 94,538.00 Pounds
VS5A VS5A
TOTAL in Current Inventory: 107,003.29 Pounds TOTAL in Previous Inventory: 101,746.08 Pounds
Naphthalene (Component of 83329/POMTV)
OS-27 0.003850 Pounds 0.004940 Pounds
ES-GEN1 ES-GEN1
ES-GEN2 ES-GEN2
TOTAL in Current Inventory: 0.00 Pounds TOTAL in Previous Inventory: 0.00 Pounds
Nitrous Oxide (N2O)
OS-3 0.002000 Tons
ES-B1 ES-B1
OS-21 0.002800 Tons
VS4A.1-ES4.1 VS4A.1-ES4.1
OS-55 0.010000 Tons 0.010000 Tons
VS5A VS5A
TOTAL in Current Inventory: 0.01 Tons TOTAL in Previous Inventory: 0.01 Tons
NOx
OS-2 0.920000 Tons 0.920000 Tons
VS4A.1-ES4.1 VS4A.1-ES4.1
OS-3 0.900000 Tons 0.880000 Tons
ES-B1 ES-B1
OS-20 1.30 Tons 1.35 Tons
VS2A-ES-2 VS2A-ES-2
OS-27 0.050000 Tons 0.070000 Tons
ES-GEN1 ES-GEN1
ES-GEN2 ES-GEN2
OS-37 0.160000 Tons 0.240000 Tons
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Bakelite Chemicals LLC - Conway
6600016 04243T27
Facility Name:
Facility ID:Permit Number(s):
Emission Rate - 2021OS ID Emission
Source ID
Pollutant
Emission Rate (Prev) - 2020
ES-B2 ES-B2
OS-54 4.65 Tons 4.52 Tons
VS5A VS5A
TOTAL in Current Inventory: 7.98 Tons TOTAL in Previous Inventory: 7.98 Tons
Phenol
OS-2 1.02 Pounds 1.00 Pounds
VS4A.1-ES4.1 VS4A.1-ES4.1
OS-12 881.20 Pounds 830.70 Pounds
VS4A.1-ES4.1 VS4A.1-ES4.1
OS-19 3.76 Pounds 3.78 Pounds
PFTF PFTF
OS-41 0.600000 Pounds 0.600000 Pounds
I-P11 I-P11
I-P12 I-P12
OS-46 1,002.57 Pounds 1,002.69 Pounds
ESR1 ESR1
ESR10 ESR10
ESR2 ESR2
ESR5 ESR5
OS-47 740.04 Pounds 740.04 Pounds
ES-PU ES-PU
OS-54 542.00 Pounds 528.00 Pounds
VS5A VS5A
TOTAL in Current Inventory: 3,171.19 Pounds TOTAL in Previous Inventory: 3,106.81 Pounds
PM(TSP)
OS-3 0.070000 Tons 0.070000 Tons
ES-B1 ES-B1
OS-20 0.100000 Tons 0.100000 Tons
VS2A-ES-2 VS2A-ES-2
OS-21 0.090000 Tons 0.050000 Tons
VS4A.1-ES4.1 VS4A.1-ES4.1
OS-35 0.010000 Tons 0.010000 Tons
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Bakelite Chemicals LLC - Conway
6600016 04243T27
Facility Name:
Facility ID:Permit Number(s):
Emission Rate - 2021OS ID Emission
Source ID
Pollutant
Emission Rate (Prev) - 2020
ES-UH-K3 ES-UH-K3
OS-36 0.010000 Tons 0.010000 Tons
ES-UH-K8 ES-UH-K8
OS-37 0.010000 Tons 0.020000 Tons
ES-B2 ES-B2
OS-48 0.150000 Tons 0.150000 Tons
ES-T1A ES-T1A
ES-T3 ES-T3
OS-49 0.210000 Tons 0.210000 Tons
ES-T1A ES-T1A
ES-T3 ES-T3
OS-50 1.12 Tons 1.19 Tons
ES-11.1 ES-11.1
ES-11.2 ES-11.2
OS-51 0.230000 Tons 0.250000 Tons
ES-11.1 ES-11.1
ES-11.2 ES-11.2
OS-52 0.230000 Tons 0.250000 Tons
ES-11.1 ES-11.1
ES-11.2 ES-11.2
OS-53 8.26 Tons 8.04 Tons
ES-MU ES-MU
I-D I-D
I-DP I-DP
I-P28 I-P28
I-R9 I-R9
I-RU1 I-RU1
I-SD1 I-SD1
I-WW1 I-WW1
VS2A-ES-FL VS2A-ES-FL
OS-55 22.81 Tons 22.55 Tons
VS5A VS5A
TOTAL in Current Inventory: 33.30 Tons TOTAL in Previous Inventory: 32.90 Tons
PM10
OS-3 0.070000 Tons 0.070000 Tons
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Bakelite Chemicals LLC - Conway
6600016 04243T27
Facility Name:
Facility ID:Permit Number(s):
Emission Rate - 2021OS ID Emission
Source ID
Pollutant
Emission Rate (Prev) - 2020
ES-B1 ES-B1
OS-20 0.100000 Tons 0.100000 Tons
VS2A-ES-2 VS2A-ES-2
OS-21 0.090000 Tons 0.050000 Tons
VS4A.1-ES4.1 VS4A.1-ES4.1
OS-35 0.010000 Tons 0.010000 Tons
ES-UH-K3 ES-UH-K3
OS-36 0.010000 Tons 0.010000 Tons
ES-UH-K8 ES-UH-K8
OS-37 0.010000 Tons 0.020000 Tons
ES-B2 ES-B2
OS-48 0.140000 Tons 0.140000 Tons
ES-T1A ES-T1A
ES-T3 ES-T3
OS-49 0.200000 Tons 0.200000 Tons
ES-T1A ES-T1A
ES-T3 ES-T3
OS-50 1.12 Tons 1.19 Tons
ES-11.1 ES-11.1
ES-11.2 ES-11.2
OS-51 0.230000 Tons 0.250000 Tons
ES-11.1 ES-11.1
ES-11.2 ES-11.2
OS-52 0.230000 Tons 0.030000 Tons
ES-11.1 ES-11.1
ES-11.2 ES-11.2
OS-53 1.65 Tons 1.61 Tons
ES-MU ES-MU
I-D I-D
I-DP I-DP
I-P28 I-P28
I-R9 I-R9
I-RU1 I-RU1
I-SD1 I-SD1
I-WW1 I-WW1
11/9/2022 Page 9 of 13
Bakelite Chemicals LLC - Conway
6600016 04243T27
Facility Name:
Facility ID:Permit Number(s):
Emission Rate - 2021OS ID Emission
Source ID
Pollutant
Emission Rate (Prev) - 2020
VS2A-ES-FL VS2A-ES-FL
OS-55 22.81 Tons 22.55 Tons
VS5A VS5A
TOTAL in Current Inventory: 26.67 Tons TOTAL in Previous Inventory: 26.23 Tons
PM2.5
OS-3 0.070000 Tons 0.070000 Tons
ES-B1 ES-B1
OS-20 0.100000 Tons 0.100000 Tons
VS2A-ES-2 VS2A-ES-2
OS-21 0.090000 Tons 0.050000 Tons
VS4A.1-ES4.1 VS4A.1-ES4.1
OS-35 0.010000 Tons 0.010000 Tons
ES-UH-K3 ES-UH-K3
OS-36 0.010000 Tons 0.010000 Tons
ES-UH-K8 ES-UH-K8
OS-37 0.010000 Tons 0.020000 Tons
ES-B2 ES-B2
OS-48 0.120000 Tons 0.120000 Tons
ES-T1A ES-T1A
ES-T3 ES-T3
OS-49 0.160000 Tons 0.160000 Tons
ES-T1A ES-T1A
ES-T3 ES-T3
OS-50 1.12 Tons 1.19 Tons
ES-11.1 ES-11.1
ES-11.2 ES-11.2
OS-51 0.230000 Tons 0.250000 Tons
ES-11.1 ES-11.1
ES-11.2 ES-11.2
OS-52 0.230000 Tons 0.030000 Tons
ES-11.1 ES-11.1
ES-11.2 ES-11.2
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Bakelite Chemicals LLC - Conway
6600016 04243T27
Facility Name:
Facility ID:Permit Number(s):
Emission Rate - 2021OS ID Emission
Source ID
Pollutant
Emission Rate (Prev) - 2020
OS-53 0.410000 Tons 0.390000 Tons
ES-MU ES-MU
I-D I-D
I-DP I-DP
I-P28 I-P28
I-R9 I-R9
I-RU1 I-RU1
I-SD1 I-SD1
I-WW1 I-WW1
VS2A-ES-FL VS2A-ES-FL
OS-55 22.81 Tons 22.55 Tons
VS5A VS5A
TOTAL in Current Inventory: 25.37 Tons TOTAL in Previous Inventory: 24.95 Tons
Polycyclic Organic Matter (Inc PAH, dioxins, etc. NC & AP 42 historic)
OS-27 0.006290 Pounds 0.008060 Pounds
ES-GEN1 ES-GEN1
ES-GEN2 ES-GEN2
TOTAL in Current Inventory: 0.01 Pounds TOTAL in Previous Inventory: 0.01 Pounds
SO2
OS-3 0.010000 Tons 0.010000 Tons
ES-B1 ES-B1
OS-20 0.010000 Tons 0.010000 Tons
VS2A-ES-2 VS2A-ES-2
OS-21 0.010000 Tons
VS4A.1-ES4.1 VS4A.1-ES4.1
OS-55 0.040000 Tons 0.030000 Tons
VS5A VS5A
TOTAL in Current Inventory: 0.07 Tons TOTAL in Previous Inventory: 0.05 Tons
Styrene
OS-54 497.00 Pounds 484.00 Pounds
VS5A VS5A
TOTAL in Current Inventory: 497.00 Pounds TOTAL in Previous Inventory: 484.00 Pounds
Toluene
11/9/2022 Page 11 of 13
Bakelite Chemicals LLC - Conway
6600016 04243T27
Facility Name:
Facility ID:Permit Number(s):
Emission Rate - 2021OS ID Emission
Source ID
Pollutant
Emission Rate (Prev) - 2020
OS-3 0.061400 Pounds 0.059700 Pounds
ES-B1 ES-B1
OS-20 0.090000 Pounds 0.090000 Pounds
VS2A-ES-2 VS2A-ES-2
OS-21 0.080000 Pounds 0.040000 Pounds
VS4A.1-ES4.1 VS4A.1-ES4.1
OS-27 0.008330 Pounds 0.010700 Pounds
ES-GEN1 ES-GEN1
ES-GEN2 ES-GEN2
OS-33 0.000020 Pounds
I-HTF I-HTF
OS-37 0.011030 Pounds 0.016410 Pounds
ES-B2 ES-B2
OS-55 0.410000 Pounds 0.370000 Pounds
VS5A VS5A
TOTAL in Current Inventory: 0.66 Pounds TOTAL in Previous Inventory: 0.59 Pounds
Triethylamine
OS-54 542.00 Pounds
VS5A VS5A
TOTAL in Current Inventory: 542.00 Pounds
VOC
OS-1 10.44 Tons 4.84 Tons
VS2A-ES-2 VS2A-ES-2
OS-2 0.130000 Tons 0.120000 Tons
VS4A.1-ES4.1 VS4A.1-ES4.1
OS-3 0.050000 Tons 0.050000 Tons
ES-B1 ES-B1
OS-12 2.75 Tons
VS4A.1-ES4.1 VS4A.1-ES4.1
OS-19 0.430000 Tons 0.420000 Tons
PFTF PFTF
11/9/2022 Page 12 of 13
Bakelite Chemicals LLC - Conway
6600016 04243T27
Facility Name:
Facility ID:Permit Number(s):
Emission Rate - 2021OS ID Emission
Source ID
Pollutant
Emission Rate (Prev) - 2020
OS-29 0.040000 Tons 0.030000 Tons
ESR8 ESR8
UFTF UFTF
OS-37 0.010000 Tons 0.010000 Tons
ES-B2 ES-B2
OS-41 0.010000 Tons 0.010000 Tons
I-P11 I-P11
I-P12 I-P12
OS-46 0.500000 Tons 0.500000 Tons
ESR1 ESR1
ESR10 ESR10
ESR2 ESR2
ESR5 ESR5
OS-47 0.370000 Tons 0.370000 Tons
ES-PU ES-PU
OS-48 10.10 Tons 10.10 Tons
ES-T1A ES-T1A
ES-T3 ES-T3
OS-49 14.03 Tons 14.03 Tons
ES-T1A ES-T1A
ES-T3 ES-T3
OS-54 56.98 Tons 54.58 Tons
VS5A VS5A
TOTAL in Current Inventory: 95.84 Tons TOTAL in Previous Inventory: 85.06 Tons
Xylene (mixed isomers)
OS-27 0.005720 Pounds 0.007340 Pounds
ES-GEN1 ES-GEN1
ES-GEN2 ES-GEN2
TOTAL in Current Inventory: 0.01 Pounds TOTAL in Previous Inventory: 0.01 Pounds
11/9/2022 Page 13 of 13
1
Drake, Alan
From:Riddick, Timothy A <[e-mail]>
Sent:Friday, November 4, 2022 8:42 AM
To:Drake, Alan
Subject:RE: [External] RE: Georgia-Pacific Chemicals - Conway CY2021 Emissions Inventory
Attachments:Calcs - DEQ Request.pdf
CAUTION: External email. Do not click links or open attachments unless you verify. Send all suspicious email as an attachment to 
Report Spam. 

Good morning Alan, 

I think that you will find this pdf. helpful to zoom in to see what you need.  If this format does not suffice or does not 
include all of the information that you would looking, please let me know. 

Thanks, 
Tim 

Tim 

Riddick

Facility Environmental Manager 

200 Ampac Rd 
Conway 

NC 

27820 

US

+1 252‐585‐3819

[e-mail]

This message, including attached files, is confidential and intended for the addressees. It may contain information that is proprietary, privileged or exempt for disclosure under applicable law. Any unauthorized use and dissemination of the 
information or copying of this message is strictly prohibited. Any views, opinions or conclusions expressed in this message are those of the individual sender and do not necessarily reflect the view of the Bakelite Synthetics group of companies 
(“Bakelite Synthetics”). If you received this message in error, please immediately advise the sender by reply email, delete all copies of this message and refrain from printing, copying, or disseminating this message or otherwise using the 
information in it. Thank you.  

Although Bakelite Synthetics routinely screens incoming and outgoing mail messages for viruses, addressees should scan this e‐mail and any attachments for viruses themselves. Bakelite Synthetics does not guarantee in any way the absence of 
viruses in this e‐mail or any attachments and disclaims any liability in case of security problem that this message may cause to any system. 

From: Drake, Alan <[e-mail]>  
Sent: Thursday, November 3, 2022 5:37 PM 
To: Riddick, Timothy A <[e-mail]> 
Subject: RE: [External] RE: Georgia‐Pacific Chemicals ‐ Conway CY2021 Emissions Inventory 

CAUTION EXTERNAL EMAIL: Please be cautious when opening links or attachments in email  

I understand, Tim. I’ve had those days too. Thanks for your attention to this matter. Alan 

2
Alan Drake 
Environmental Engineer, Division of Air Quality 
North Carolina Department of Environmental Quality 
1641 Mail Service Center, Raleigh, NC 27699 
Office: (919) 707‐8493 
[e-mail] 

From: Riddick, Timothy A <[e-mail]>  
Sent: Thursday, November 3, 2022 5:32 PM 
To: Drake, Alan <[e-mail]> 
Subject: [External] RE: Georgia‐Pacific Chemicals ‐ Conway CY2021 Emissions Inventory 

CAUTION: External email. Do not click links or open attachments unless you verify. Send all suspicious email as an attachment to 
Report Spam. 

Mr. Drake, 

It’s been one of those days so I apologize for not replying earlier.  I will get you the requested information as soon as 
possible tomorrow if that is acceptable. 

Thanks, 
Tim 

Tim 

Riddick

Facility Environmental Manager 

200 Ampac Rd 
Conway 

NC 

27820 

US

+1 252‐585‐3819

[e-mail]

This message, including attached files, is confidential and intended for the addressees. It may contain information that is proprietary, privileged or exempt for disclosure under applicable law. Any unauthorized use and dissemination of the 
information or copying of this message is strictly prohibited. Any views, opinions or conclusions expressed in this message are those of the individual sender and do not necessarily reflect the view of the Bakelite Synthetics group of companies 
(“Bakelite Synthetics”). If you received this message in error, please immediately advise the sender by reply email, delete all copies of this message and refrain from printing, copying, or disseminating this message or otherwise using the 
information in it. Thank you.  

Although Bakelite Synthetics routinely screens incoming and outgoing mail messages for viruses, addressees should scan this e‐mail and any attachments for viruses themselves. Bakelite Synthetics does not guarantee in any way the absence of 
viruses in this e‐mail or any attachments and disclaims any liability in case of security problem that this message may cause to any system. 

3
From: Drake, Alan <[e-mail]>  
Sent: Thursday, November 3, 2022 9:26 AM 
To: Riddick, Timothy A <[e-mail]> 
Subject: Georgia‐Pacific Chemicals ‐ Conway CY2021 Emissions Inventory 
Importance: High 

CAUTION EXTERNAL EMAIL: Please be cautious when opening links or attachments in email  

November 3, 2022 

Tim, 

I’m currently reviewing the subject emissions inventory, dated May 20, 2022, and am having a very difficult time reading 
the attachments. I’ve tried scanning and zooming in on some items but they become pixelated and unreadable 
especially if they’re on a colored background. The last 12 pages, beginning with boiler ES‐B1 are legible but the previous 
pages are not. 

If you could email me the spreadsheets for the first dozen pages attached to the letter, I’d appreciate it.  

Best regards, 
Alan 

Alan Drake 
Environmental Engineer, Division of Air Quality 
North Carolina Department of Environmental Quality 
1641 Mail Service Center, Raleigh, NC 27699 
Office: (919) 707‐8493 
[e-mail] 

1.
i.
ii.
2.
3.

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:

For a corporation: a president, secretary, treasurer, or vice-president of the corporation in charge of a principal business
function, or any other person who performs similar policy or decision making functions for the overall operation of one or
more manufacturing, production, or operating facilities applying for a or subject to a permit and either
the facilities employ more than 250 persons or have gross annual sales or expenditures exceeding $25 million(in
second quarter 1980 dollars); or
the delegation of authority to such representatives is approved in advance by the permitting authority;
For partnership or sole proprietorship; a general partner or the proprietor, respectively;
For a municipality, state, federal, or other public agency includes the chief executive officer having responsibility for the
overall operations of a principal geographic unit of the agency (e.g., a Regional Administrator of EPA).

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
Inventory Certification Form(Title V)
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO

North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
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 Robert Dalton
This person or one that meets the definition below must sign this certification form.
CERTIFICATION STATEMENT:
(Important: Legally Responsible Official, read and sign after all submissions are final.)
I certify that I am the responsible official for this facility, as described above, and hereby certify that the information contained in
this air emissions report, including attached calculations and documentation, is true, accurate and complete. (Subject to legal
penalties of up to $25,000 per occurrence and possible imprisonment as outlined in G.S. § 143-215.3(a)(2))
Responsible Official's Signature Below (use blue ink): Date Signed:
Printed Name: Robert Dalton
Signature:
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.
Email address of Responsible Official:[e-mail]
Information on this Form cannot be held confidential
COPY of RECORD Date Submitted: 5/20/2022 08:34:49

1

Listing of Emission Sources and Control Devices on Permit. See instructions

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
*ES ID on
Air Permit
*ES Description *CS ID *CS Description * CD ID's
ES-11.1 Extender storage silo RM3
ES-11.2 Extender storage silo RM4
ES-B1
One natural gas/propane-fired boiler
(25.1 million Btu per hour maximum
heat input rate) [NSPS Dc, MACT
DDDDD]

ES-B2
One natural gas-fired temporary
boiler (less than 25 million Btu per
hour maximum heat input rate)
[NSPS Dc, MACT DDDDD]

ES-GEN1
Diesel-fired generator (500 kW
maximum rated power output)
[MACT ZZZZ]

ES-GEN2
Diesel-fired generator (500 kW
maximum rated power output)
[MACT ZZZZ]

ES-MU Methanol tank truck/railcar unloading
ES-PU Phenol unloading operations [MACT
OOO, MACT UU]
ES-RLR
Resin loading racks comprised of
emissions from East Load Rack,
West Load Rack, Reactor Load Rack,
and Railcar Load Rack

ES-S19
Aqueous ammonia storage tank
(9,924 gallon capacity) [MACT
OOO, MACT UU]
CS-6 One scrubber tank (56 inch minimum water
level from tank bottom), CD-S19
ES-T1A Cooling Tower HX1 (432,000 gallons
per hour capacity) [MACT F]
ES-T3 Cooling Tower HX2 (600,000 gallons
per hour capacity) [MACT OOO]
ES-UH-K3 Urea unloading hopper for reactor #3
ES-UH-K8 Urea unloading hopper for reactor #8
ES4.6 Batch non-reactor vessel, mix/blend
tank K6 [MACT OOO, MACT UU]
ESR1 Phenol storage tank (22,548 gallon
capacity) [MACT OOO, MACT UU]
ESR10 Phenol storage tank (22,548 gallon
capacity) [MACT OOO, MACT UU]
ESR2 Phenol storage tank (22,548 gallon
capacity) [MACT OOO, MACT UU]
ESR5 Phenol storage tank (22,548 gallon
capacity) [MACT OOO, MACT UU]
2
ESR8
Urea-formaldehyde concentrate
(UFC) storage tank (25,366 gallon
capacity) [MACT OOO, MACT UU]

I-A2 Methyl ethyl ketone tank (9,910
gallon capacity)
I-C1 Sulfuric acid tank (5,000 gallon
capacity)
I-C2 GP-4590 Pre-catalyst tank (5,000
gallon capacity)
I-C3 GP-4590 Pre-catalyst tank (5,000
gallon capacity)
I-CF Resin loading operations - Container
loading
I-D Diesel fuel dispenser rack
I-D1 Diesel fuel tank (12,000 gallon
capacity)
I-D2 Diesel fuel tank (10,000 gallon
capacity)
I-DP Solid resins drying pad
I-FA Formic acid tank (2,610 gallon
capacity)
I-FL Formaldehyde loading operations -
East Load Rack
I-G1 Gasoline tank (2,000 gallon capacity)
I-HTF
Natural gas/propane-fired heat
transfer fluid heater (2.3 million Btu
per hour maximum heat input rate)

I-HTF1 Heat transfer fluid tank (2,800 gallon
capacity)
I-MU Methanol/formaldehyde unloading
I-N1 PF resin tank (22,559 gallon
capacity)
I-N2 PF resin tank (22,559 gallon
capacity)
I-N3 PF resin tank (22,559 gallon
capacity)
I-N4 PF resin tank (22,559 gallon
capacity)
I-N5 PF resin tank (22,559 gallon
capacity)
I-N6 PF resin tank (22,559 gallon
capacity)
I-N7 PF resin tank (22,559 gallon
capacity)
I-NMO New motor oil tank (500 gallon
capacity)
I-P1 PF RESI-MIX resin tank (25,908
gallon capacity)
I-P10 PF RESI-MIX resin tank (25,908
gallon capacity)
I-P11 PF RESI-MIX resin tank (25,908
gallon capacity)
I-P12 PF RESI-MIX resin tank (25,908
gallon capacity)
I-P13 PF resin tank (22,669 gallon
capacity)
I-P14 PF resin tank (22,669 gallon
capacity)
3
I-P15 PF resin tank (22,669 gallon
capacity)
I-P17 PF resin tank (22,669 gallon
capacity)
I-P19 PF resin tank (22,669 gallon
capacity)
I-P2 PF RESI-MIX resin tank (25,908
gallon capacity)
I-P20 PF resin tank (22,669 gallon
capacity)
I-P21 PF resin tank (22,669 gallon
capacity)
I-P22 PF resin tank (22,669 gallon
capacity)
I-P23 PF resin tank (22,669 gallon
capacity)
I-P24 PF Resin tank (22,669 gallon
capacity)
I-P25 PF resin tank (22,669 gallon
capacity)
I-P26 PF resin tank (22,669 gallon
capacity)
I-P27 PF resin tank (22,669 gallon
capacity)
I-P28 PF resin tank (22,669 gallon
capacity)
I-P3 PF RESI-MIX resin tank (25,908
gallon capacity)
I-P30 Process water tank (2,560 gallon
capacity)
I-P4 PF RESI-MIX resin tank (25,908
gallon capacity)
I-P5 PF RESI-MIX resin tank (25,908
gallon capacity)
I-P6 PF RESI-MIX resin tank (25,908
gallon capacity)
I-P7 PF RESI-MIX resin tank (25,908
gallon capacity)
I-P8 PF RESI-MIX resin tank (25,908
gallon capacity)
I-P9 PF RESI-MIX resin tank (25,908
gallon capacity)
I-PR-1 Paved Roads
I-R1.21B Phenol tank (22,540 gallon capacity)
I-R10.21B Phenol tank (22,540 gallon capacity)
I-R2.21B Phenol tank (22,540 gallon capacity)
I-R3 Cresylic acid tank (22,669 gallon
capacity)
I-R4 Caustic soda tank (29,500 gallon
capacity)
I-R5.21B Phenol tank (22,540 gallon capacity)
I-R6 Process water tank (19,000 gallon
capacity)
I-R7 Urea solution tank (19,431 gallon
capacity)
I-R8.21B Urea formaldehyde concentrate tank
(25,379 gallon capacity)
4
I-R9 Process water tank (29,000 gallon
capacity)
I-RMCT1 Resi-Mix Chill Tank (6,141 gallon
capacity)
I-RU1 Granular urea railcar screw conveyor
unloading
I-RUR Resin unloading rack No. 7
I-S1 PF flammable resin tank (9,910
gallon capacity)
I-S11 PF flammable resin tank (9,910
gallon capacity)
I-S12 PF flammable resin tank (9,910
gallon capacity)
I-S14 PF specialty resins tank (9,910 gallon
capacity)
I-S15 PF specialty resins tank (9,910 gallon
capacity)
I-S16 PF specialty resins tank (9,910 gallon
capacity)
I-S17 PF specialty resins tank (9,910 gallon
capacity)
I-S18 PF specialty resins tank (9,910 gallon
capacity)
I-S2 PF flammable resin tank (9,910
gallon capacity)
I-S20 Distillate water tank (9,910 gallon
capacity)
I-S21 PF specialty resins tank (9,910 gallon
capacity)
I-S22 PF specialty resins tank (9,910 gallon
capacity)
I-S3 PF flammable resin tank (9,910
gallon capacity)
I-S4 PF flammable resin tank (9,910
gallon capacity)
I-S5 PF flammable resin tank (9,910
gallon capacity)
I-S6 PF flammable resin tank (9,910
gallon capacity)
I-S7 PF flammable resin tank (9,910
gallon capacity)
I-S8 PF flammable resin tank (9,910
gallon capacity)
I-S9 PF flammable resin tank (9,910
gallon capacity)
I-SD1 Truck unloading of spray dry material
I-U1 PF flammable resin tank (22,443
gallon capacity)
I-U10 UF resin tank (22,443 gallon
capacity)
I-U2 PF flammable resin tank (22,443
gallon capacity)
I-U3 PF flammable resin tank (22,443
gallon capacity)
I-U4 UF resin tank (22,443 gallon
capacity)
I-U5 UF resin tank (22,443 gallon
capacity)
5
I-U6 UF resin tank (22,443 gallon
capacity)
I-U7 UF resin tank (22,443 gallon
capacity)
I-U8 UF resin tank (22,443 gallon
capacity)
I-U9 UF resin tank (22,443 gallon
capacity)
I-UMO Used motor oil tank (500 gallon
capacity)
I-WW1 Process water tank (27,678 gallon
capacity)
I-WW2 Process water tank (12,500 gallon
capacity)
ICT-1 PF RESI-MIX resin tank (27,663
gallon capacity)
ICT-2 PF RESI-MIX resin tank (27,663
gallon capacity)
ISD-1 PF resin tank (27,663 gallon
capacity)
ISD-2 PF resin tank (27,663 gallon
capacity)
PFTF Phenol-formaldehyde resin tank farm
[MACT OOO, MACT UU]
UFTF Urea-formaldehyde resin tank farm
[MACT OOO, MACT UU]
VS2A-ES-2
One formaldehyde production
process including vaporizers,
catalytic converters, cooling systems,
an after cooler and an absorber
[MACT F, MACT G, MACT H]
CS-1 Catalytic incinerator (4.5 cf of catalyst,
propane fired 4.0 MBtu/hr primary burner CD-2A
VS2A-ES-
FL
One formaldehyde tank truck loading
rack
VS2A-
ES3M1
One methanol storage tank (507,852
gallon capacity) when this source is
operating under its primary
compliance scenario [MACT F,
MACT G, MACT H]
CS-1 Catalytic incinerator (4.5 cf of catalyst,
propane fired 4.0 MBtu/hr primary burner CD-2A
VS2A-
ES7F1
One formaldehyde/methanol storage
tank (26,212 gallon capacity) when
operating under the primary
compliance scenario [MACT F,
MACT G, MACT H]
CS-1 Catalytic incinerator (4.5 cf of catalyst,
propane fired 4.0 MBtu/hr primary burner CD-2A
VS2A-
ES7F2
One formaldehyde/methanol storage
tank (26,212 gallon capacity) when
operating under the primary
compliance scenario [MACT F,
MACT G, MACT H]
CS-1 Catalytic incinerator (4.5 cf of catalyst,
propane fired 4.0 MBtu/hr primary burner CD-2A
VS2A-
ES7F3
One formaldehyde/methanol storage
tank (26,212 gallon capacity) when
operating under the primary
compliance scenario [MACT F,
MACT G, MACT H]
CS-1 Catalytic incinerator (4.5 cf of catalyst,
propane fired 4.0 MBtu/hr primary burner CD-2A
VS2A-
ES7F4
One formaldehyde/methanol storage
tank (26,212 gallon capacity) when
operating under the primary
compliance scenario [MACT F,
MACT G, MACT H]
CS-1 Catalytic incinerator (4.5 cf of catalyst,
propane fired 4.0 MBtu/hr primary burner CD-2A
6
VS2A-
ES7F5
One formaldehyde/methanol storage
tank (26,212 gallon capacity) when
operating under the primary
compliance scenario [MACT F,
MACT G, MACT H]
CS-1 Catalytic incinerator (4.5 cf of catalyst,
propane fired 4.0 MBtu/hr primary burner CD-2A
VS2A-
ES7F6
One formaldehyde/methanol storage
tank (26,212 gallon capacity) when
operating under the primary
compliance scenario [MACT F,
MACT G, MACT H]
CS-1 Catalytic incinerator (4.5 cf of catalyst,
propane fired 4.0 MBtu/hr primary burner CD-2A
VS2A-
ES7F7
One formaldehyde/methanol storage
tank (26,212 gallon capacity) when
operating under the primary
compliance scenario [MACT F,
MACT G, MACT H]
CS-1 Catalytic incinerator (4.5 cf of catalyst,
propane fired 4.0 MBtu/hr primary burner CD-2A
VS2A-
ES7F8
One formaldehyde/methanol storage
tank (26,212 gallon capacity) when
operating under the primary
compliance scenario [MACT F,
MACT G, MACT H]
CS-1 Catalytic incinerator (4.5 cf of catalyst,
propane fired 4.0 MBtu/hr primary burner CD-2A
VS4A.1-ES-
13
one mix/blend tank [MACT OOO,
MACT UU]
VS4A.1-
ES4.1
Batch reactor vessel [MACT OOO,
MACT UU] CS-2 Thermal oxidizer (propane/natural gas fired
2.9 million Btu per hour) CD-4A
VS4A.1-
ES4.1-5WT
Batch non-reactor vessel (weigh tank)
[MACT OOO, MACT UU]
VS4A.1-
ES4.2
Batch reactor vessel [MACT OOO,
MACT UU]
VS4A.1-
ES4.2WT
Batch non-reactor vessel (weigh tank)
[MACT OOO, MACT UU]
VS4A.1-
ES4.3
Batch reactor vessel [MACT OOO,
MACT UU]
VS4A.1-
ES4.5
Batch reactor vessel [MACT OOO,
MACT UU]
VS4A.1-
ES4.7
Batch reactor vessel [MACT OOO,
MACT UU]
VS4A.1-
ES4.8
Batch reactor vessel [MACT OOO,
MACT UU]
VS4A.1-
ES4.8WT
Batch non-reactor vessel (weigh tank)
[MACT OOO, MACT UU]
VS4A.2-ES-
13
one mix/blend tank [MACT OOO,
MACT UU]
VS4A.2-
ES3M1
One methanol storage tank (507,852
gallon capacity) when this source is
operating under its alternate
compliance scenario [MACT F,
MACT G, MACT H]

VS4A.2-
ES4.1
Batch reactor vessel [MACT OOO,
MACT UU]
VS4A.2-
ES4.1-5WT
Batch non-reactor vessel (weigh tank)
[MACT OOO, MACT UU]
VS4A.2-
ES4.2
Batch reactor vessel [MACT OOO,
MACT UU]
VS4A.2-
ES4.2WT
Batch non-reactor vessel (weigh tank)
[MACT OOO, MACT UU]
VS4A.2-
ES4.3
Batch reactor vessel [MACT OOO,
MACT UU]
VS4A.2-
ES4.5
Batch reactor vessel [MACT OOO,
MACT UU]
7

VS4A.2-
ES4.7
Batch reactor vessel [MACT OOO,
MACT UU]
VS4A.2-
ES4.8
Batch reactor vessel [MACT OOO,
MACT UU]
VS4A.2-
ES4.8WT
Batch non-reactor vessel (weigh tank)
[MACT OOO, MACT UU]
VS4A.2-
ES7F1
One formaldehyde/methanol storage
tank (26,212 gallon capacity) when
operating under the alternate
compliance scenario [MACT F,
MACT G, MACT H]

VS4A.2-
ES7F2
One formaldehyde/methanol storage
tank (26,212 gallon capacity) when
operating under the alternate
compliance scenario [MACT F,
MACT G, MACT H]

VS4A.2-
ES7F3
One formaldehyde/methanol storage
tank (26,212 gallon capacity) when
operating under the alternate
compliance scenario [MACT F,
MACT G, MACT H]

VS4A.2-
ES7F4
One formaldehyde/methanol storage
tank (26,212 gallon capacity) when
operating under the alternate
compliance scenario [MACT F,
MACT G, MACT H]

VS4A.2-
ES7F5
One formaldehyde/methanol storage
tank (26,212 gallon capacity) when
operating under the alternate
compliance scenario [MACT F,
MACT G, MACT H]

VS4A.2-
ES7F6
One formaldehyde/methanol storage
tank (26,212 gallon capacity) when
operating under the alternate
compliance scenario [MACT F,
MACT G, MACT H]

VS4A.2-
ES7F7
One formaldehyde/methanol storage
tank (26,212 gallon capacity) when
operating under the alternate
compliance scenario [MACT F,
MACT G, MACT H]

VS4A.2-
ES7F8
One formaldehyde/methanol storage
tank (26,212 gallon capacity) when
operating under the alternate
compliance scenario [MACT F,
MACT G, MACT H]

VS5A
Continuous process vent stream
comprised of emissions from the
spray dry resin production process
including a natural gas/propane-fired
atomizing air heater (14.6 million Btu
per hour maximum heat input rate), a
spray dryer, several transfer cyclones
and a product bagging operation (No.
ES-5) [CAM, MACT OOO, MACT
UU]
CS-3 Bagfilter (18,600 sf of filter area), Bagfilter
(1000 sf of filter area) CD-5A

8

Emission Source & Operating Scenario List - See Instructions

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
*ES Group ID *ES ID *OS ID *OS Description
GR92
VS2A-ES7F1, VS2A-
ES7F2, VS2A-ES7F3,
VS2A-ES7F4, VS2A-
ES7F5, VS2A-ES7F6,
VS2A-ES7F7, VS2A-ES7F8
13 Formaldehdyde Raw Material Storage
Tanks
GR93 ESR1, ESR10, ESR2, ESR5 46 Phenol Raw Material Storage Tanks
GR95 ESR8, UFTF 29 Urea Formaldehyde Resin Storage Tanks
G-105 ES-GEN1, ES-GEN2 27 Industrial engines
GR163 I-P11, I-P12 41
Phenol-Formaldehyde Resin Storage
Tanks
GR166
ES-MU, I-D, I-DP, I-P28, I-
R9, I-RU1, I-SD1, I-WW1,
VS2A-ES-FL
53 Paved Roads (PR-1)
GR181 ES-T1A, ES-T3
48 Cooling Tower (ES-T1A)
49 Cooling Tower (ES-T3)
GR186 ES-11.1, ES-11.2
50 RESI-MIXER® (ES4.6)
51 RM3 Extender Storage Silo (ES-11.1)
52 RM4 Extender Storage Silo (ES-11.2)
ES-B1 3
Natural gas/propane fired boiler (25.1
MMBtu/hr heat input)
ES-B2 37
Temporary Boiler - Used only when on-
site boiler is to be out of service for
extended period.
ES-PU 47 Fugitive emissions from phenol unloading
ES-RLR NONE NONE
ES-S19 40 Aqueous ammonia storage tank
ES-UH-K3 35 Urea Hopper for Reactor #3
ES-UH-K8 36 Urea Hopper for Reactor #8
ES4.6 NONE NONE
I-A2 44 MEK Usage
I-C1 NONE NONE
I-C2 NONE NONE
I-C3 NONE NONE
I-CF NONE NONE
I-D1 NONE NONE
I-D2 NONE NONE
I-FA NONE NONE
I-FL NONE NONE
I-G1 NONE NONE
I-HTF 33 DowTherm Heater
9
I-HTF1 NONE NONE
I-MU NONE NONE
I-N1 NONE NONE
I-N2 NONE NONE
I-N3 NONE NONE
I-N4 NONE NONE
I-N5 NONE NONE
I-N6 NONE NONE
I-N7 NONE NONE
I-NMO NONE NONE
I-P1 NONE NONE
I-P10 NONE NONE
I-P13 NONE NONE
I-P14 NONE NONE
I-P15 NONE NONE
I-P17 NONE NONE
I-P19 NONE NONE
I-P2 NONE NONE
I-P20 NONE NONE
I-P21 NONE NONE
I-P22 NONE NONE
I-P23 NONE NONE
I-P24 NONE NONE
I-P25 NONE NONE
I-P26 NONE NONE
I-P27 NONE NONE
I-P3 NONE NONE
I-P30 NONE NONE
I-P4 NONE NONE
I-P5 NONE NONE
I-P6 NONE NONE
I-P7 NONE NONE
I-P8 NONE NONE
I-P9 NONE NONE
I-PR-1 NONE NONE
I-R1.21B NONE NONE
I-R10.21B NONE NONE
I-R2.21B NONE NONE
I-R3 NONE NONE
I-R4 NONE NONE
I-R5.21B NONE NONE
I-R6 NONE NONE
I-R7 NONE NONE
I-R8.21B NONE NONE
I-RMCT1 NONE NONE
I-RUR NONE NONE
I-S1 NONE NONE
I-S11 NONE NONE
I-S12 NONE NONE
I-S14 NONE NONE
I-S15 NONE NONE
I-S16 NONE NONE
I-S17 NONE NONE
10
I-S18 NONE NONE
I-S2 NONE NONE
I-S20 NONE NONE
I-S21 NONE NONE
I-S22 NONE NONE
I-S3 NONE NONE
I-S4 NONE NONE
I-S5 NONE NONE
I-S6 NONE NONE
I-S7 NONE NONE
I-S8 NONE NONE
I-S9 NONE NONE
I-U1 NONE NONE
I-U10 NONE NONE
I-U2 NONE NONE
I-U3 NONE NONE
I-U4 NONE NONE
I-U5 NONE NONE
I-U6 NONE NONE
I-U7 NONE NONE
I-U8 NONE NONE
I-U9 NONE NONE
I-UMO NONE NONE
I-WW2 NONE NONE
ICT-1 NONE NONE
ICT-2 NONE NONE
ISD-1 NONE NONE
ISD-2 NONE NONE
PFTF 19 Phenol-Formaldehyde Resin Storage Tank
VS2A-ES-2
1 Formaldehyde manufacturing
10 Fugitive Sources - LDAR, etc.
20 Natural Gas Usage for Catalytic Oxidizer
VS2A-ES3M1 15 Methanol Raw Material Storage Tank
VS4A.1-ES-13 NONE NONE
VS4A.1-ES4.1
2 Resin manufacturing with eight kettles and
seven weigh tanks
12 Fugitive Sources - LDAR, Loading Racks,
Drying Pad
21 Natural Gas Usage for thermal oxidizer
VS4A.1-ES4.1-5WT NONE NONE
VS4A.1-ES4.2 NONE NONE
VS4A.1-ES4.2WT NONE NONE
VS4A.1-ES4.3 NONE NONE
VS4A.1-ES4.5 NONE NONE
VS4A.1-ES4.7 NONE NONE
VS4A.1-ES4.8 NONE NONE
VS4A.1-ES4.8WT NONE NONE
VS4A.2-ES-13 NONE NONE
VS4A.2-ES3M1 NONE NONE
VS4A.2-ES4.1 NONE NONE
VS4A.2-ES4.1-5WT NONE NONE
VS4A.2-ES4.2 NONE NONE
VS4A.2-ES4.2WT NONE NONE
11
VS4A.2-ES4.3 NONE NONE
VS4A.2-ES4.5 NONE NONE
VS4A.2-ES4.7 NONE NONE
VS4A.2-ES4.8 NONE NONE
VS4A.2-ES4.8WT NONE NONE
VS4A.2-ES7F1 NONE NONE
VS4A.2-ES7F2 NONE NONE
VS4A.2-ES7F3 NONE NONE
VS4A.2-ES7F4 NONE NONE
VS4A.2-ES7F5 NONE NONE
VS4A.2-ES7F6 NONE NONE
VS4A.2-ES7F7 NONE NONE
VS4A.2-ES7F8 NONE NONE
VS5A 54 Spray Dry Resin Manufacturing
55 Natural gas usage in spray dry process

12

8. Control Device Information :

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
Group GR92 consisting of VS2A-ES7F1, VS2A-ES7F2, VS2A-ES7F3,
VS2A-ES7F4, VS2A-ES7F5, VS2A-ES7F6, VS2A-ES7F7, VS2A-
ES7F8
2. Emission Source Description :Formaldehyde Storage Tanks
3. Operating Scenario ID/
Description:
OS - 13/Formaldehdyde Raw Material Storage Tanks
4. SCC Number/Description:40799999/Miscellaneous ; Other Not Classified

5. Throughput/units in 2021:
(e.g. production or fuel use):
14169818 GAL/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
100
Order CS-ID CD ID
(as listed in permit)
Control Device Description
1 CS-1 CD-2A Natural gas/propane-fired catalytic oxidizer (4.5 cubic feet of
catalyst, 4.0 million Btu per hour maximum heat input primary
burner)

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
E401 VERTICAL
STACK 36 1.5 700 33 3500
Formaldehyde
process plant
catalytic oxidizer
13

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 13 Emission Source/Group ID: GR92
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 08 0
NOx NOx 08 0
TSP TSP 08 0
PM10 PM10 08 0
PM2.5 PM2.5 08 0
SO2 SO2 08 0
VOC VOC 0 08 99.99 0 BEFORE
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021
Formaldehyde 50-00-0 0 02 99.99 0 AFTER
Methanol 67-56-1 0 02 99.99 0 AFTER

15

8. Control Device Information :None

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
Group GR93 consisting of ESR1, ESR10, ESR2, ESR5
2. Emission Source Description :Phenol Storage Tanks
3. Operating Scenario ID/
Description:
OS - 46/Phenol Raw Material Storage Tanks
4. SCC Number/Description:40708404/Fixed Roof Tanks - Phenols ; Phenol: Working Loss

5. Throughput/units in 2021:
(e.g. production or fuel use):
8312830 GAL/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):

Order CS-ID CD ID
(as listed in permit)
Control Device Description

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
Raw Ma FUGITIVE (NO
STACK) 1 72 Area = 1
Raw Material
fugitive tank
emissiona

16

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 46 Emission Source/Group ID: GR93
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
SO2 SO2 08
VOC VOC 0.5 08
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021
Phenol 108-95-2 1002.57 08

17

8. Control Device Information :None

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
Group GR95 consisting of ESR8, UFTF
2. Emission Source Description :Urea-Formaldehyde Storage Tanks
3. Operating Scenario ID/
Description:
OS - 29/Urea Formaldehyde Resin Storage Tanks
4. SCC Number/Description:40714698/Fixed Roof Tanks - Miscellaneous ; Specify In Comments:
Working Loss

5. Throughput/units in 2021:
(e.g. production or fuel use):
1542292 GAL/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):

Order CS-ID CD ID
(as listed in permit)
Control Device Description

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
Fugitive FUGITIVE (NO
STACK) 1 77 Area = 1 Fugitive Releases

18

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 29 Emission Source/Group ID: GR95
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
SO2 SO2 08
VOC VOC 0.04 02
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021
Formaldehyde 50-00-0 36.84 02
Methanol 67-56-1 32.66 02

19

8. Control Device Information :None

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
Group G-105 consisting of ES-GEN1, ES-GEN2
2. Emission Source Description :Industrial engines
3. Operating Scenario ID/
Description:
OS - 27/Industrial engines
4. SCC Number/Description:20100107/Distillate Oil (Diesel) ; Reciprocating: Exhaust

5. Throughput/units in 2021:
(e.g. production or fuel use):
215 GAL/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):

Order CS-ID CD ID
(as listed in permit)
Control Device Description

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
E111-2 VERTICAL
STACK 17 0.5 855 365.41 4305 Generator stack

20

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 27 Emission Source/Group ID: G-105
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 0.01 08
NOx NOx 0.05 08
TSP TSP 008
PM10 PM10 008
PM2.5 PM2.5 008
SO2 SO2 008
VOC VOC 008
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021
Acetaldehyde 75-07-0 0.00075 08
Acrolein 107-02-8 0.00023 08
Benzene 71-43-2 0.023 08
Formaldehyde 50-00-0 0.00234 08
Naphthalene (Component
of POMTV)91-20-3 0.00385 08
Polycyclic Organic Matter
(Inc PAH, dioxins, etc. NC
& AP 42 historic
amorphous glob)
POM 0.00629 08
Toluene 108-88-3 0.00833 08
Xylene 1330-20-7 0.00572 08

21

8. Control Device Information :None

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
Group GR163 consisting of I-P11, I-P12
2. Emission Source Description :Phenol-Formaldehyde Resin Storage Tanks
3. Operating Scenario ID/
Description:
OS - 41/Phenol-Formaldehyde Resin Storage Tanks
4. SCC Number/Description:40799999/Miscellaneous ; Other Not Classified

5. Throughput/units in 2021:
(e.g. production or fuel use):
2381178 GAL/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):

Order CS-ID CD ID
(as listed in permit)
Control Device Description

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
Fugitive FUGITIVE (NO
STACK) 1 77 Area = 1 Fugitive Releases

22

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 41 Emission Source/Group ID: GR163
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
SO2 SO2 08
VOC VOC 0.01 08
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021
Formaldehyde 50-00-0 1.5 08
Methanol 67-56-1 10.31 08
Phenol 108-95-2 0.6 08

23

8. Control Device Information :None

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
Group GR166 consisting of ES-MU, I-D, I-DP, I-P28, I-R9, I-RU1, I-
SD1, I-WW1, VS2A-ES-FL
2. Emission Source Description :Insignificant Sources
3. Operating Scenario ID/
Description:
OS - 53/Paved Roads (PR-1)
4. SCC Number/Description:31499999/Other Not Classified ; Other Not Classified

5. Throughput/units in 2021:
(e.g. production or fuel use):
1 EACH/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):

Order CS-ID CD ID
(as listed in permit)
Control Device Description

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
Fugitive FUGITIVE (NO
STACK) 1 77 Area = 1 Fugitive Releases

24

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 53 Emission Source/Group ID: GR166
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 08
NOx NOx 08
TSP TSP 8.26 08
PM10 PM10 1.65 08
PM2.5 PM2.5 0.41 08
SO2 SO2 08
VOC VOC 08
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021

25

8. Control Device Information :None

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
Group GR181 consisting of ES-T1A, ES-T3
2. Emission Source Description :Cooling Towers
3. Operating Scenario ID/
Description:
OS - 48/Cooling Tower (ES-T1A)
4. SCC Number/Description:39999995/Miscellaneous Industrial Processes ; Other Not Classified

5. Throughput/units in 2021:
(e.g. production or fuel use):
1 EACH/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):

Order CS-ID CD ID
(as listed in permit)
Control Device Description

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
Fugitive FUGITIVE (NO
STACK) 1 77 Area = 1 Fugitive Releases

26

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 48 Emission Source/Group ID: GR181
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 08
NOx NOx 08
TSP TSP 0.15 08
PM10 PM10 0.14 08
PM2.5 PM2.5 0.12 08
SO2 SO2 08
VOC VOC 10.1 08
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021

27

8. Control Device Information :None

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
Group GR181 consisting of ES-T1A, ES-T3
2. Emission Source Description :Cooling Towers
3. Operating Scenario ID/
Description:
OS - 49/Cooling Tower (ES-T3)
4. SCC Number/Description:39999995/Miscellaneous Industrial Processes ; Other Not Classified

5. Throughput/units in 2021:
(e.g. production or fuel use):
1 EACH/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):

Order CS-ID CD ID
(as listed in permit)
Control Device Description

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
Fugitive FUGITIVE (NO
STACK) 1 77 Area = 1 Fugitive Releases

28

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 49 Emission Source/Group ID: GR181
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 08
NOx NOx 08
TSP TSP 0.21 08
PM10 PM10 0.2 08
PM2.5 PM2.5 0.16 08
SO2 SO2 08
VOC VOC 14.03 08
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021

29

8. Control Device Information :None

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
Group GR186 consisting of ES-11.1, ES-11.2
2. Emission Source Description :Resi-Mixer
3. Operating Scenario ID/
Description:
OS - 50/RESI-MIXER® (ES4.6)
4. SCC Number/Description:30199998/*Other Organic Chemica Manufacture Not Listed ; Specify in
Comments Field

5. Throughput/units in 2021:
(e.g. production or fuel use):
1 EACH/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):

Order CS-ID CD ID
(as listed in permit)
Control Device Description

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
K-6 BH
6.1
VERTICAL
STACK 2 1.4 77 41.57 3840
K-6 Baghouse
Exhaust

30

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 50 Emission Source/Group ID: GR186
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 08
NOx NOx 08
TSP TSP 1.12 08
PM10 PM10 1.12 08
PM2.5 PM2.5 1.12 08
SO2 SO2 08
VOC VOC 08
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021

31

8. Control Device Information :None

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
Group GR186 consisting of ES-11.1, ES-11.2
2. Emission Source Description :Resi-Mixer
3. Operating Scenario ID/
Description:
OS - 51/RM3 Extender Storage Silo (ES-11.1)
4. SCC Number/Description:30199998/*Other Organic Chemica Manufacture Not Listed ; Specify in
Comments Field

5. Throughput/units in 2021:
(e.g. production or fuel use):
1 EACH/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):

Order CS-ID CD ID
(as listed in permit)
Control Device Description

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
RM-3
CD11.1
VERTICAL
STACK 1.5 1.67 77 6.08 800 RM-3 Bin Vent

32

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 51 Emission Source/Group ID: GR186
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 08
NOx NOx 08
TSP TSP 0.23 08
PM10 PM10 0.23 08
PM2.5 PM2.5 0.23 08
SO2 SO2 08
VOC VOC 08
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021

33

8. Control Device Information :None

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
Group GR186 consisting of ES-11.1, ES-11.2
2. Emission Source Description :Resi-Mixer
3. Operating Scenario ID/
Description:
OS - 52/RM4 Extender Storage Silo (ES-11.2)
4. SCC Number/Description:30199998/*Other Organic Chemica Manufacture Not Listed ; Specify in
Comments Field

5. Throughput/units in 2021:
(e.g. production or fuel use):
1 EACH/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):

Order CS-ID CD ID
(as listed in permit)
Control Device Description

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
RM-4
CD-11.2
VERTICAL
STACK 2.78 1.67 77 6.08 800 RM-4 Bin Vent

34

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 52 Emission Source/Group ID: GR186
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 08
NOx NOx 08
TSP TSP 0.23 08
PM10 PM10 0.23 08
PM2.5 PM2.5 0.23 08
SO2 SO2 08
VOC VOC 08
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021

35

8. Control Device Information :None

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
ES-B1
2. Emission Source Description :One natural gas/propane-fired boiler (25.1 million Btu per hour
maximum heat input rate) [NSPS Dc]
3. Operating Scenario ID/
Description:
OS - 3/Natural gas/propane fired boiler (25.1 MMBtu/hr heat input)
4. SCC Number/Description:10200602/Natural Gas ; 10-100 Million Btu/hr

5. Throughput/units in 2021:
(e.g. production or fuel use):
18051 E3FT3/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):

Order CS-ID CD ID
(as listed in permit)
Control Device Description

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
E201 VERTICAL
STACK 36 2.67 367 19.8 6651.64 boiler group stack

36

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 3 Emission Source/Group ID: ES-B1
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
Carbon Dioxide (CO2) 124389 1076.93 08
Methane (CH4) 74-82-8 0.02 08
Nitrous Oxide (N2O) 10024972 0.002 08

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 0.76 08
NOx NOx 0.9 08
TSP TSP 0.07 08
PM10 PM10 0.07 08
PM2.5 PM2.5 0.07 08
SO2 SO2 0.01 08
VOC VOC 0.05 08
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021
Benzene 71-43-2 0.0379 08
Formaldehyde 50-00-0 1.35 08
Hexane, n- 110-54-3 32.49 08
Toluene 108-88-3 0.0614 08

37

8. Control Device Information :None

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
ES-B2
2. Emission Source Description :One natural gas/propane/No. 2 fuel oil-fired temporary boiler (less than
25 million Btu per hour maximum heat input rate) [NSPS Dc]
3. Operating Scenario ID/
Description:
OS - 37/Temporary Boiler - Used only when on-site boiler is to be out of
service for extended period.
4. SCC Number/Description:10300602/Natural Gas ; 10-100 Million Btu/hr

5. Throughput/units in 2021:
(e.g. production or fuel use):
3243 E3FT3/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):

Order CS-ID CD ID
(as listed in permit)
Control Device Description

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
E201 VERTICAL
STACK 36 2.67 367 19.8 6651.64 boiler group stack

38

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 37 Emission Source/Group ID: ES-B2
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
Carbon Dioxide (CO2) 124389 193 08

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 0.14 08
NOx NOx 0.16 08
TSP TSP 0.01 08
PM10 PM10 0.01 08
PM2.5 PM2.5 0.01 08
SO2 SO2 008
VOC VOC 0.01 08
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021
Benzene 71-43-2 0.00681 08
Formaldehyde 50-00-0 0.24322 08
Hexane, n- 110-54-3 5.83737 08
Toluene 108-88-3 0.01103 08

39

8. Control Device Information :None

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
ES-PU
2. Emission Source Description :Phenol unloading operations [MACT OOO, MACT UU]
3. Operating Scenario ID/
Description:
OS - 47/Fugitive emissions from phenol unloading
4. SCC Number/Description:31499999/Other Not Classified ; Other Not Classified

5. Throughput/units in 2021:
(e.g. production or fuel use):
78473113 LB/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):

Order CS-ID CD ID
(as listed in permit)
Control Device Description

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
EP-PU VERTICAL
STACK 13.2 2 160 0.1 18.84
Phenol Unloading
Process

40

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 47 Emission Source/Group ID: ES-PU
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
SO2 SO2 08
VOC VOC 0.37 02
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021
Phenol 108-95-2 740.04 02

41

8. Control Device Information :

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
ES-S19
2. Emission Source Description :Aqueous ammonia storage tank (9,924 gallon capacity) [MACT OOO,
MACT UU]
3. Operating Scenario ID/
Description:
OS - 40/Aqueous ammonia storage tank
4. SCC Number/Description:40714698/Fixed Roof Tanks - Miscellaneous ; Specify In Comments:
Working Loss

5. Throughput/units in 2021:
(e.g. production or fuel use):
703953 GAL/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
100
Order CS-ID CD ID
(as listed in permit)
Control Device Description
1 CS-6 CD-S19 One scrubber tank (56 inch minimum water level from tank bottom)

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
S-19
Tank
Vent
VERTICAL
STACK 15 1 77 1 47.12 Tank Vent

42

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 40 Emission Source/Group ID: ES-S19
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 08 0
NOx NOx 08 0
TSP TSP 08 0
PM10 PM10 08 0
PM2.5 PM2.5 08 0
SO2 SO2 08 0
VOC VOC 08 0
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021
Ammonia (as NH3) 7664-41-7 278.66 08 75 BEFORE

43

8. Control Device Information :None

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
ES-UH-K3
2. Emission Source Description :Urea unloading hopper for reactor #3
3. Operating Scenario ID/
Description:
OS - 35/Urea Hopper for Reactor #3
4. SCC Number/Description:40799999/Miscellaneous ; Other Not Classified

5. Throughput/units in 2021:
(e.g. production or fuel use):
14273876 LB/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):

Order CS-ID CD ID
(as listed in permit)
Control Device Description

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
EP-K3A FUGITIVE (NO
STACK) 1 72 Area = 1
Exhaust from Urea
Hopper for Reactor
#3

44

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 35 Emission Source/Group ID: ES-UH-K3
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 08
NOx NOx 08
TSP TSP 0.01 08
PM10 PM10 0.01 08
PM2.5 PM2.5 0.01 08
SO2 SO2 08
VOC VOC 08
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021

45

8. Control Device Information :None

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
ES-UH-K8
2. Emission Source Description :Urea unloading hopper for reactor #8
3. Operating Scenario ID/
Description:
OS - 36/Urea Hopper for Reactor #8
4. SCC Number/Description:40799999/Miscellaneous ; Other Not Classified

5. Throughput/units in 2021:
(e.g. production or fuel use):
19569046 LB/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):

Order CS-ID CD ID
(as listed in permit)
Control Device Description

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
EP-K8A FUGITIVE (NO
STACK) 1 72 Area = 1
Exhaust from urea
hopper for Reactor
#8

46

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 36 Emission Source/Group ID: ES-UH-K8
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 08
NOx NOx 08
TSP TSP 0.01 08
PM10 PM10 0.01 08
PM2.5 PM2.5 0.01 08
SO2 SO2 08
VOC VOC 08
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021

47

8. Control Device Information :None

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
I-A2
2. Emission Source Description :Acetone distillate tank (9,924 gallon capacity)
3. Operating Scenario ID/
Description:
OS - 44/MEK Usage
4. SCC Number/Description:40706806/Fixed Roof Tanks - Ketones ; Methyl Ethyl Ketone: Working
Loss

5. Throughput/units in 2021:
(e.g. production or fuel use):
19851 GAL/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):

Order CS-ID CD ID
(as listed in permit)
Control Device Description

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
STK-A2 DOWNWARD-
FACING VENT 1 0.25 70 0.1 0.29
I-A2 MEK Storage
Tank Vent

48

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 44 Emission Source/Group ID: I-A2
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
SO2 SO2 08
VOC VOC 008
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021
Methyl ethyl ketone 78-93-3 0.74 02

49

8. Control Device Information :None

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
I-HTF
2. Emission Source Description :Natural gas/propane-fired heat transfer fluid heater (2.3 million Btu per
hour maximum heat input rate)
3. Operating Scenario ID/
Description:
OS - 33/DowTherm Heater
4. SCC Number/Description:10300602/Natural Gas ; 10-100 Million Btu/hr

5. Throughput/units in 2021:
(e.g. production or fuel use):
7 E3FT3/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):

Order CS-ID CD ID
(as listed in permit)
Control Device Description

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
DowThe
rm
Heater
VERTICAL
STACK 35 1 350 31.83 1500
Dowtherm Heater
Exhaust

50

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 33 Emission Source/Group ID: I-HTF
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
Carbon Dioxide (CO2) 124389 0.4 08
Nitrous Oxide (N2O) 10024972 008

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 008
NOx NOx 008
TSP TSP 008
PM10 PM10 008
PM2.5 PM2.5 008
SO2 SO2 008
VOC VOC 008
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021
Benzene 71-43-2 0.00001 08
Formaldehyde 50-00-0 0.0005 08
Hexane, n- 110-54-3 0.01 08
Toluene 108-88-3 0.00002 08

51

8. Control Device Information :None

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
PFTF
2. Emission Source Description :Phenol-formaldehyde resin tank farm [MACT OOO, MACT UU]
3. Operating Scenario ID/
Description:
OS - 19/Phenol-Formaldehyde Resin Storage Tank
4. SCC Number/Description:30199998/*Other Organic Chemica Manufacture Not Listed ; Specify in
Comments Field

5. Throughput/units in 2021:
(e.g. production or fuel use):
40818321 GAL/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):

Order CS-ID CD ID
(as listed in permit)
Control Device Description

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
Fugitive FUGITIVE (NO
STACK) 1 77 Area = 1 Fugitive Releases

52

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 19 Emission Source/Group ID: PFTF
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
SO2 SO2 08
VOC VOC 0.43 04
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021
Formaldehyde 50-00-0 15.01 04
Methanol 67-56-1 837.21 04
Phenol 108-95-2 3.76 04

53

8. Control Device Information :

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
VS2A-ES-2
2. Emission Source Description :One formaldehyde production process including vaporizers, catalytic
converters, cooling systems, an after cooler and an absorber [MACT F,
MACT G, MACT H]
3. Operating Scenario ID/
Description:
OS - 1/Formaldehyde manufacturing
4. SCC Number/Description:30112002/Formaldahyde, Acrolein, Acetaldehyde, Butyraldehyde MFG ;
Formaldehyde: Mixed Oxide Catalyst

5. Throughput/units in 2021:
(e.g. production or fuel use):
13150360 GAL/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
100
Order CS-ID CD ID
(as listed in permit)
Control Device Description
1 CS-1 CD-2A Natural gas/propane-fired catalytic oxidizer (4.5 cubic feet of
catalyst, 4.0 million Btu per hour maximum heat input primary
burner)

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
E401 VERTICAL
STACK 36 1.5 700 33 3500
Formaldehyde
process plant
catalytic oxidizer
54

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 1 Emission Source/Group ID: VS2A-ES-
2
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 4.57 08 98.6 AFTER
NOx NOx 08 0
TSP TSP 08 0
PM10 PM10 08 0
PM2.5 PM2.5 08 0
SO2 SO2 08 0
VOC VOC 10.44 08 98.6 AFTER
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021
Acetaldehyde 75-07-0 20.13 04 98.6 AFTER
Formaldehyde 50-00-0 3037.89 04 98.6 AFTER
Methanol 67-56-1 2558.32 04 98.6 AFTER

56

8. Control Device Information :None

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
VS2A-ES-2
2. Emission Source Description :One formaldehyde production process including vaporizers, catalytic
converters, cooling systems, an after cooler and an absorber [MACT F,
MACT G, MACT H]
3. Operating Scenario ID/
Description:
OS - 10/Fugitive Sources - LDAR, etc.
4. SCC Number/Description:30112002/Formaldahyde, Acrolein, Acetaldehyde, Butyraldehyde MFG ;
Formaldehyde: Mixed Oxide Catalyst

5. Throughput/units in 2021:
(e.g. production or fuel use):
1 EACH/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):

Order CS-ID CD ID
(as listed in permit)
Control Device Description

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
Fugitive FUGITIVE (NO
STACK) 1 77 Area = 1 Fugitive Releases

57

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 10 Emission Source/Group ID: VS2A-ES-
2
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
SO2 SO2 08
VOC VOC 08
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021
Formaldehyde 50-00-0 150 02
Methanol 67-56-1 716 02

58

8. Control Device Information :None

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
VS2A-ES-2
2. Emission Source Description :One formaldehyde production process including vaporizers, catalytic
converters, cooling systems, an after cooler and an absorber [MACT F,
MACT G, MACT H]
3. Operating Scenario ID/
Description:
OS - 20/Natural Gas Usage for Catalytic Oxidizer
4. SCC Number/Description:30112002/Formaldahyde, Acrolein, Acetaldehyde, Butyraldehyde MFG ;
Formaldehyde: Mixed Oxide Catalyst

5. Throughput/units in 2021:
(e.g. production or fuel use):
25995 E3FT3/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):

Order CS-ID CD ID
(as listed in permit)
Control Device Description

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
E401 VERTICAL
STACK 36 1.5 700 33 3500
Formaldehyde
process plant
catalytic oxidizer

59

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 20 Emission Source/Group ID: VS2A-ES-
2
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
Carbon Dioxide (CO2) 124389 2290.78 08
Methane (CH4) 74-82-8 0.03 08

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 08
NOx NOx 1.3 08
TSP TSP 0.1 08
PM10 PM10 0.1 08
PM2.5 PM2.5 0.1 08
SO2 SO2 0.01 08
VOC VOC 08
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021
Benzene 71-43-2 0.05 08
Hexane, n- 110-54-3 46.79 08
Toluene 108-88-3 0.09 08

60

8. Control Device Information :

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
VS2A-ES3M1
2. Emission Source Description :One methanol storage tank (507,852 gallon capacity) when this source is
operating under its primary compliance scenario [MACT F, MACT G,
MACT H]
3. Operating Scenario ID/
Description:
OS - 15/Methanol Raw Material Storage Tank
4. SCC Number/Description:40700816/Fixed Roof Tanks - Alcohols ; Methyl Alcohol: Working Loss

5. Throughput/units in 2021:
(e.g. production or fuel use):
11587854 GAL/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
100
Order CS-ID CD ID
(as listed in permit)
Control Device Description
1 CS-1 CD-2A Natural gas/propane-fired catalytic oxidizer (4.5 cubic feet of
catalyst, 4.0 million Btu per hour maximum heat input primary
burner)

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
E401 VERTICAL
STACK 36 1.5 700 33 3500
Formaldehyde
process plant
catalytic oxidizer
61

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 15 Emission Source/Group ID: VS2A-
ES3M1
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 08 0
NOx NOx 08 0
TSP TSP 08 0
PM10 PM10 08 0
PM2.5 PM2.5 08 0
SO2 SO2 08 0
VOC VOC 0 08 99.99 0 BEFORE
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021
Methanol 67-56-1 0 08 99.99 0 BEFORE

63

8. Control Device Information :

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
VS4A.1-ES4.1
2. Emission Source Description :Batch reactor vessel [MACT OOO, MACT UU]
3. Operating Scenario ID/
Description:
OS - 2/Resin manufacturing with eight kettles and seven weigh tanks
4. SCC Number/Description:30199998/*Other Organic Chemica Manufacture Not Listed ; Specify in
Comments Field

5. Throughput/units in 2021:
(e.g. production or fuel use):
324298106 LB/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
100
Order CS-ID CD ID
(as listed in permit)
Control Device Description
1 CS-2 CD-4A Natural gas/propane-fired thermal oxidizer (2.9 million Btu per hour
maximum heat input)

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
E501-8 VERTICAL
STACK 20 0.5 91 8.82 104 Thermal Oxidizer

64

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 2 Emission Source/Group ID: VS4A.1-
ES4.1
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 4.18 08 0
NOx NOx 0.92 08 0
TSP TSP 08 0
PM10 PM10 08 0
PM2.5 PM2.5 08 0
SO2 SO2 08 0
VOC VOC 0.13 08 98 AFTER
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021
Formaldehyde 50-00-0 22.29 04 96 AFTER
Methanol 67-56-1 228.49 04 99 AFTER
Phenol 108-95-2 1.02 04 97.5 AFTER

65

8. Control Device Information :None

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
VS4A.1-ES4.1
2. Emission Source Description :Batch reactor vessel [MACT OOO, MACT UU]
3. Operating Scenario ID/
Description:
OS - 12/Fugitive Sources - LDAR, Loading Racks, Drying Pad
4. SCC Number/Description:30199998/*Other Organic Chemica Manufacture Not Listed ; Specify in
Comments Field

5. Throughput/units in 2021:
(e.g. production or fuel use):
1 EACH/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):

Order CS-ID CD ID
(as listed in permit)
Control Device Description

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
Fugitive FUGITIVE (NO
STACK) 1 77 Area = 1 Fugitive Releases

66

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 12 Emission Source/Group ID: VS4A.1-
ES4.1
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
SO2 SO2 08
VOC VOC 2.75 08
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021
Ammonia (as NH3) 7664-41-7 36.77 08
Cresol (mixed isomers) 1319-77-3 108.1 02
Formaldehyde 50-00-0 534.1 02
Methanol 67-56-1 3790.3 02
Methyl ethyl ketone 78-93-3 194.59 08
Phenol 108-95-2 881.2 02

67

8. Control Device Information :None

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
VS4A.1-ES4.1
2. Emission Source Description :Batch reactor vessel [MACT OOO, MACT UU]
3. Operating Scenario ID/
Description:
OS - 21/Natural Gas Usage for thermal oxidizer
4. SCC Number/Description:30199998/*Other Organic Chemica Manufacture Not Listed ; Specify in
Comments Field

5. Throughput/units in 2021:
(e.g. production or fuel use):
24472 E3FT3/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):

Order CS-ID CD ID
(as listed in permit)
Control Device Description

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
E501-8 VERTICAL
STACK 20 0.5 91 8.82 104 Thermal Oxidizer

68

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 21 Emission Source/Group ID: VS4A.1-
ES4.1
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
Carbon Dioxide (CO2) 124389 1503.43 08
Methane (CH4) 74-82-8 008
Nitrous Oxide (N2O) 10024972 0.0028 08

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 08
NOx NOx 08
TSP TSP 0.09 08
PM10 PM10 0.09 08
PM2.5 PM2.5 0.09 08
SO2 SO2 0.01 08
VOC VOC 08
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021
Benzene 71-43-2 0.05 08
Hexane, n- 110-54-3 44.05 08
Toluene 108-88-3 0.08 08

69

8. Control Device Information :

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
VS5A
2. Emission Source Description :Continuous process vent stream comprised of emissions from the spray
dry resin production process including a natural gas/propane-fired
atomizing air heater (14.6 million Btu per hour maximum heat inp
3. Operating Scenario ID/
Description:
OS - 54/Spray Dry Resin Manufacturing
4. SCC Number/Description:30190003/*Fuel Fired Process Equipment ; Natural Gas: Process Heaters

5. Throughput/units in 2021:
(e.g. production or fuel use):
34649858 LB/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):
100
Order CS-ID CD ID
(as listed in permit)
Control Device Description
1 CS-3 CD-5A Bagfilter (14,500 square feet of filter area)

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
e131 VERTICAL
STACK 110 6 160 29.47 50000
Spray Dry
Operations

70

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 54 Emission Source/Group ID: VS5A
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 11.41 08 0
NOx NOx 4.65 08 0
TSP TSP 08 99
PM10 PM10 08 99
PM2.5 PM2.5 08 99
SO2 SO2 08 0
VOC VOC 56.98 08 0
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021
Acetaldehyde 75-07-0 226 08 0
Ammonia (as NH3) 7664-41-7 320 04 0
Cresol (mixed isomers) 1319-77-3 858 08 0
Formaldehyde 50-00-0 8488 04 0
Methanol 67-56-1 98830 04 0
Phenol 108-95-2 542 04 0
Styrene 100-42-5 497 04 0
Triethylamine 121-44-8 542 08 0

71

8. Control Device Information :None

9. Emission Release Point (ERP) Information: (Sources vented to more than one ERP use additional entry lines):

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
1. Emission Source ID (from permit)
or Emission Source Group ID
VS5A
2. Emission Source Description :Continuous process vent stream comprised of emissions from the spray
dry resin production process including a natural gas/propane-fired
atomizing air heater (14.6 million Btu per hour maximum heat inp
3. Operating Scenario ID/
Description:
OS - 55/Natural gas usage in spray dry process
4. SCC Number/Description:30190003/*Fuel Fired Process Equipment ; Natural Gas: Process Heaters

5. Throughput/units in 2021:
(e.g. production or fuel use):
120046 E3FT3/yr
6. Fuel Information
(If fuel is used)
%Sulfur

%Ash

Heat Content
(Btu/units)

7. Capture Efficiency
(% of Emissions from this Process Vented
to Control Device or Stack):

Order CS-ID CD ID
(as listed in permit)
Control Device Description

ERP ID ERP Type Height
(in feet)
Diameter
Circle (enter #):
Rectangle (L x W)
(in 0.1 feet)
Temperature
(F)
Velocity
(Feet/sec)
Volume Flow
Rate (Acfm)
ERP Description
e131 VERTICAL
STACK 110 6 160 29.47 50000
Spray Dry
Operations

72

10. Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2021)
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:

13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.

Operating Scenario: OS - 55 Emission Source/Group ID: VS5A
Jan-Feb + Dec
2021 25%March-May
2021 25%June-Aug.
2021 25%Sept.-Nov.
2021 25%
GHG
Pollutants CAS
Emissions-
GHG
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
Carbon Dioxide (CO2) 124389 7161.89 08
Methane (CH4) 74-82-8 0.13 08
Nitrous Oxide (N2O) 10024972 0.01 08

Criteria
(NAAQS)
Pollutants
Pollutant
Code
Emissions-
Criteria
Pollutants
(Tons/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after
all controls)
Emission
Factor
Ef
Control
2021
CO CO 08
NOx NOx 08
TSP TSP 22.81 08
PM10 PM10 22.81 08
PM2.5 PM2.5 22.81 08
SO2 SO2 0.04 08
VOC VOC 08
HAP/TAP
Pollutants (In Alphabetical Order)
CAS
(see instructions)
Emissions
HAP/TAPS
(Pounds/Year)
Emission
Estimation
Method Code
(See Instructions)
Control
Efficiency
(Net after all controls)
Emission
Factor
EF
Control
2021
Benzene 71-43-2 0.25 08
Hexane, n- 110-54-3 216.08 08
Toluene 108-88-3 0.41 08

73

Record Facility-Wide Totals From all Permitted and Non-Permitted AirPollutant Emission Sources

Facility Total CY 2021 Emissions Summary

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory - Calendar Year 2021
Green House Gases Pollutants(GHG)
Actual Emissions (Tons/Year)
Pollutant CAS 2021 2020 % Change
Carbon Dioxide (CO2) 124389 12226.43 10839.12 12.799097%
Methane (CH4) 74-82-8 0.18 .18 0.0%
Nitrous Oxide (N2O) 10024972 0.0148 .01 48.000004%
Criteria Pollutants
Actual Emissions (Tons/Year)
Pollutant CAS 2021 2020 % Change
CO CO 21.07 30.04 -29.86019%
NOx NOx 7.98 7.98 0.0%
PM(TSP) TSP 33.3 32.9 1.2157985%
PM10 PM10 26.67 26.23 1.6774706%
PM2.5 PM2.5 25.37 24.95 1.683367%
SO2 SO2 0.07 .05 40.0%
VOC VOC 95.84 85.06 12.673406%
Hazardous Air Pollutants(HAPS) and/or Toxic Air Pollutants(TAPs)
Actual Emissions (Pounds/Year)
Pollutant CAS 2021 2020 % Change
Pollutant Group:Polycyclic Organic Matter (Specific Compounds from OAQPS for TV) Group Sum:.00385
Naphthalene (Component of
POMTV)91-20-3 0.00385 .00494 -22.064775%
Acetaldehyde 75-07-0 246.13075 238.70096 3.112595%
Acrolein 107-02-8 2.3E-4 .0003 -23.333336%
Ammonia (as NH3) 7664-41-7 635.43 616.66 3.04382%
Benzene 71-43-2 0.41772 .39653 5.343855%
Cresol (mixed isomers) 1319-77-3 966.1 935.9 3.2268353%
Formaldehyde 50-00-0 12287.226 11776.35493 4.338109%
Hexane, n- 110-54-3 345.2574 304.88635 13.241338%
Methanol 67-56-1 107003.29 101746.08 5.1669917%
Methyl ethyl ketone 78-93-3 195.33 196.11 -0.39773533%
74
Phenol 108-95-2 3171.19 3106.81 2.0722182%
Polycyclic Organic Matter (Inc
PAH, dioxins, etc. NC & AP 42
historic amorphous glob)
POM 0.00629 .00806 -21.960299%
Styrene 100-42-5 497.0 484 2.6859505%
Toluene 108-88-3 0.66078 .58681 12.605447%
Triethylamine 121-44-8 542.0 Not reported N/A
Xylene 1330-20-7 0.00572 .00734 -22.070848%

75

COPY of RECORD Date Submitted: 5/20/2022 08:34:49
As entered in AERO
Facility Name: Georgia-Pacific Chemicals LLC - Conway
200 Ampac Road
Conway, NC 27820

Facility ID : 6600016
Permit : 04243
County : Northampton
DAQ Region : RRO
Comments From Facility:

76
Tanks Emissions Estimates
Calendar Year: 2021RY Yellow = User Must Check Each Year Template Owner: Divisional Environmental Manager
Plant Location: Conway, NC AP-42, 7-1 Organic Liquid Storage Tanks 59.2833 F = daily average ambient temperature (Taa) Blue = User Linked to Other Tab (Typically Production)Version: 1.02
21.7167 F = daily ambient temperature range (dTa) (F or R) Green = User Must Review and Confirm Accuracy
1,393.0797 = Solar Index Gray = Locked Calculation or Constant Columns AX through AZ are hidden and contain intermediate calculations & values ==>
14.53 psi = ambient pressure (psi) Others = If input, may be entered, but should typically be constant.
Tank or Tank Group Product or Description
Paint Factor (see table
below)
Tank Dia
(Ft)
Tank
Ht. (Ft)Max. Liq. Ht (Ft)Avg. Liq. Ht
(Ft)Cone or Dome Dome Height
(ft)
Tank Shell
Capacity (Gal)
Tank
Working
Volume (Gal)
Liquid Temp
(F or Amb)
Product Density
(lb/gal)
TOTAL Throughput
(Gal)# Tanks Throughput (Gal /
Tank)
Controlled
Temp?
(% Eff.)
Vapor
Collection?
(% Eff.)
Vapor
Return?
(% Eff.)
Conservation
Vent dP (psi)
(pres - vac)
Chemical Percent of Free
Chemical MW
Partial vp at
Storage
Condition
(psi)
Controlled Working
Loss
(lb per tank)
Controlled
Breathing Loss
(lb per tank)
Controlled
TOTAL Losses
(all tanks) A B C
Calc. partial vapor
pressure (based on
Tla)
N
Turnovers
per tank
Kn Calculated Working
Losses (lbs)
Calculated Standing
Losses (lbs)
Hvo Hro Vv Wv Tb dTv
Tla (
R )Tlx Tln Pvx Pvn dPv
F1-F8 HCHO Soln. - HCHO 0.17 12 31 15.5 Cone 1.0 26,225 26,225 145 9.12 14,169,818 8 1,771,227 100% 100% HCHO 50.00%30 0.35519 <=HCHO Eq.0.00 0.00 0.00 na na na 0.35519 67.5 0.611 274.50 38.08 15.833 0.333 1,790.71 0.0016422 518.9733 22.2671 604.67 610.23677 599.10323 0.42600 0.29514 0.13086
F1-F8 HCHO Soln. - MeOH 0.17 12 31 15.5 Cone 1.0 26,225 26,225 145 9.12 14,169,818 8 1,771,227 100% 100% MeOH 0.40%32.04 0.05440 <=Calc Antoine 0.00 0.00 0.00 7.897 1474.1 229.13 0.05440 67.5 0.611 44.90 6.34 15.833 0.333 1,790.71 0.0002686 518.9733 22.2671 604.67 610.23677 599.10323 0.06146 0.04803 0.01342
R-8 UFC Soln. - HCHO 0.17 12 30 15.0 Cone 1.0 25,379 25,379 100 11.04 685,141 1 685,141 100% HCHO 30.00%30 0.05890 <=HCHO Eq.28.83 0.00 28.83 na na na 0.05890 27.0 1.000 28.83 7.38 15.333 0.333 1,734.16 0.0002942 518.9733 22.2671 559.67 565.23677 554.10323 0.07282 0.04744 0.02537
R-8 UFC Soln. - MeOH 0.17 12 30 15.0 Cone 1.0 25,379 25,379 100 11.04 685,141 1 685,141 100% MeOH 0.40%32.04 0.01831 <=Calc Antoine 9.57 0.00 9.57 7.897 1474.1 229.13 0.01831 27.0 1.000 9.57 2.45 15.333 0.333 1,734.16 9.767E-05 518.9733 22.2671 559.67 565.23677 554.10323 0.02118 0.01577 0.00541
M-1 Methanol 0.17 46.5 40 20.0 Cone 1.0 508,104 508,104 Amb 6.63 11,587,854 1 11,587,854 100% .06 psi MeOH 100.00%32.04 1.49589 <=Calc Antoine 0.00 0.00 0.00 7.897 1474.1 229.13 1.49589 22.8 1.000 13,223.73 3,239.96 20.333 0.333 34,530.70 0.0085753 518.9733 22.2671 520.835 526.40218 515.26864 1.77705 1.25369 0.52336
R-1, R-2
R-5, R-10 Phenol 0.17 10.5 34.8
17.4 Cone 1.0 22,540 22,540 145 9.44 8,312,830 4 2,078,207 100% Phenol 100.00%94.1 0.10940 <=Calc Antoine 250.64 0.00 1,002.57 7.133 1516.8 174.95 0.10940 92.2 0.492 250.64 32.04 17.733 0.333 1,535.54 0.0015865 518.9733 22.2671 604.67 610.23677 599.10323 0.13212 0.09014 0.04198
S-19 Aqua Ammonia
(adjusted to 28%)0.17 10.5 15.3 7.7 Cone 1.0 9,910 9,910 50 7.48 703,953 1 703,953 100% 75% Ammonia 30.00%17.03 6.63000 <=Enter vp 278.66 0.00 278.66 N/A N/A N/A 0.00000 71.0 0.589 1,114.63 704.38 7.983 0.333 691.28 0.0206442 518.9733 22.2671 509.67 515.23677 504.10323 Hand CalcHand Calc=>3.72000
<=Hand Enter!
C-1 Sulfuric Acid 0.17 8 12.33 6.2 Cone 1.0 4,636 4,636 85 10.40 0 1 0 100% .06 psi NON VOC 0.00000 <=Enter vp 0.00 0.00 0.00 N/A N/A N/A 0.00000 0.0 1.000 0.00 0.00 6.498 0.333 326.64 0 518.9733 22.2671 544.67 550.23677 539.10323 Hand CalcHand Calc=>0.10000
C-2 CCKC- 902G03 (NON VOC)0.17 8 12.33 6.2 Cone 1.0 4,636 4,636 85 10.40 0 1 0 100% .06 psi NON VOC 0.00000 <=Enter vp 0.00 0.00 0.00 N/A N/A N/A 0.00000 0.0 1.000 0.00 0.00 6.498 0.333 326.64 0 518.9733 22.2671 544.67 550.23677 539.10323 Hand CalcHand Calc=>0.10000
C-3 CCKC- 902G03 (NON VOC)0.17 8 12.33 6.2 Cone 1.0 4,636 4,636 85 10.40 0 1 0 100% .06 psi NON VOC 0.00000 <=Enter vp 0.00 0.00 0.00 N/A N/A N/A 0.00000 0.0 1.000 0.00 0.00 6.498 0.333 326.64 0 518.9733 22.2671 544.67 550.23677 539.10323 Hand CalcHand Calc=>0.10000
CT-1, 2, SD-1,2 (Spray
Dry Base)PF Resin - HCHO 0.17 12 32.7 16.4 Cone 1.0 27,663 27,663 55 10.40 6,422,204 4 1,605,551 100% HCHO 0.50%30 0.00075 <=HCHO Eq.0.59 0.00 2.35 na na na 0.00075 58.0 0.684 0.59 0.12 16.683 0.333 1,886.84 4.074E-06 518.9733 22.2671 514.67 520.23677 509.10323 0.00096 0.00058 0.00038
CT-1, 2, SD-1,2 (Spray
Dry Base)PF Resin - Phenol 0.17 12 32.7
16.4 Cone 1.0 27,663 27,663 55 10.40 6,422,204 4 1,605,551 100% Phenol 1.00%94.1 0.00002 <=Calc Antoine 0.05 0.00 0.22 7.133 1516.8 174.95 0.00002 58.0 0.684 0.05 0.01 16.683 0.333 1,886.84 3.725E-07 518.9733 22.2671 514.67 520.23677 509.10323 0.00003 0.00002 0.00001
CT-1, 2, SD-1,2 (Spray
Dry Base)PF Resin - MeOH 0.17 12 32.7 16.4 Cone 1.0 27,663 27,663 55 10.40 6,422,204 4 1,605,551 100% MeOH 0.10%32.04 0.00123 <=Calc Antoine 1.03 0.00 4.12 7.897 1474.1 229.13 0.00123 58.0 0.684 1.03 0.21 16.683 0.333 1,886.84 7.134E-06 518.9733 22.2671 514.67 520.23677 509.10323 0.00147 0.00103 0.00044
N1-N7
(Resi-Mix Base)PF Resin - HCHO 0.17 10.5 34.83
17.4 Cone 1.0 22,559 22,559 80 10.40 8,764,556 7 1,252,079 100% HCHO 0.20%30 0.00089 <=HCHO Eq.0.56 0.00 3.93 na na na 0.00089 55.5 0.707 0.56 0.11 17.748 0.333 1,536.83 4.599E-06 518.9733 22.2671 539.67 545.23677 534.10323 0.00112 0.00070 0.00041
N1-N7
(Resi-Mix Base)PF Resin - Phenol 0.17 10.5 34.83 17.4 Cone 1.0 22,559 22,559 80 10.40 8,764,556 7 1,252,079 100% Phenol 0.20%94.1 0.00002 <=Calc Antoine 0.03 0.00 0.22 7.133 1516.8 174.95 0.00002 55.5 0.707 0.03 0.01 17.748 0.333 1,536.83 2.559E-07 518.9733 22.2671 539.67 545.23677 534.10323 0.00002 0.00001 0.00001
N1-N7
(Resi-Mix Base)PF Resin - MeOH 0.17 10.5 34.83
17.4 Cone 1.0 22,559 22,559 80 10.40 8,764,556 7 1,252,079 100% MeOH 0.50%32.04 0.01317 <=Calc Antoine 8.90 0.00 62.28 7.897 1474.1 229.13 0.01317 55.5 0.707 8.90 1.68 17.748 0.333 1,536.83 7.287E-05 518.9733 22.2671 539.67 545.23677 534.10323 0.01543 0.01120 0.00424
Resi-Mixer (K-6)PF Resin - HCHO 0.17 9 11 5.5 Cone 1.0 5,234 5,234 80 10.40 10,955,695 1 10,955,695 HCHO 0.30%30 0.00133 <=HCHO Eq.1.89 0.04 1.92 na na na 0.00133 2,093.0 0.181 1.89 0.04 5.833 0.333 371.10 6.898E-06 518.9733 22.2671 539.67 545.23677 534.10323 0.00167 0.00106 0.00062
Resi-Mixer (K-6)PF Resin - Phenol 0.17 9 11
5.5 Cone 1.0 5,234 5,234 80 10.40 10,955,695 1 10,955,695 Phenol 0.00%94.1 0.00000 <=Calc Antoine 0.00 0.00 0.00 7.133 1516.8 174.95 0.00000 2,093.0 0.181 0.00 0.00 5.833 0.333 371.10 0 518.9733 22.2671 539.67 545.23677 534.10323 0.00000 0.00000 0.00000
Resi-Mixer (K-6)PF Resin - MeOH 0.17 9 11 5.5 Cone 1.0 5,234 5,234 80 10.40 10,955,695 1 10,955,695 MeOH 0.00%32.04 0.00000 <=Calc Antoine 0.00 0.00 0.00 7.897 1474.1 229.13 0.00000 2,093.0 0.181 0.00 0.00 5.833 0.333 371.10 0 518.9733 22.2671 539.67 545.23677 534.10323 0.00000 0.00000 0.00000
P1-P6, P8-P10
(Resimix)PF Resin - HCHO 0.17 10.5 32.0
16.0 Cone 1.0 20,726 20,726 80 10.40 11,130,426 9 1,236,714 100% HCHO 0.20%30 0.00089 <=HCHO Eq.0.52 0.00 4.72 na na na 0.00089 59.7 0.669 0.52 0.10 16.333 0.333 1,414.31 4.599E-06 518.9733 22.2671 539.67 545.23677 534.10323 0.00112 0.00070 0.00041
P1-P6, P8-P10
(Resimix)PF Resin - Phenol 0.17 10.5 32.0 16.0 Cone 1.0 20,726 20,726 80 10.40 11,130,426 9 1,236,714 100% Phenol 0.20%94.1 0.00002 <=Calc Antoine 0.03 0.00 0.26 7.133 1516.8 174.95 0.00002 59.7 0.669 0.03 0.01 16.333 0.333 1,414.31 2.559E-07 518.9733 22.2671 539.67 545.23677 534.10323 0.00002 0.00001 0.00001
P1-P6, P8-P10
(Resimix)PF Resin - MeOH 0.17 10.5 32.0
16.0 Cone 1.0 20,726 20,726 80 10.40 11,130,426 9 1,236,714 100% MeOH 0.50%32.04 0.01317 <=Calc Antoine 8.32 0.00 74.87 7.897 1474.1 229.13 0.01317 59.7 0.669 8.32 1.55 16.333 0.333 1,414.31 7.287E-05 518.9733 22.2671 539.67 545.23677 534.10323 0.01543 0.01120 0.00424
P11-P12 (WW Tanks) PF Resin - HCHO
0.17 10.5 35.0 17.5 Cone 1.0 22,669 22,669 80 10.40 529,151 2 264,575 HCHO 0.20%30 0.00089 <=HCHO Eq.0.17 0.11 0.55 na na na 0.00089 11.7 1.000 0.17 0.11 17.833 0.333 1,544.19 4.599E-06 518.9733 22.2671 539.67 545.23677 534.10323 0.00112 0.00070 0.00041
P11-P12 (WW Tanks) PF Resin - Phenol
0.17 10.5 35.0
17.5 Cone 1.0 22,669 22,669 80 10.40 529,151 2 264,575 Phenol 1.50%94.1 0.00012 <=Calc Antoine 0.07 0.04 0.23 7.133 1516.8 174.95 0.00012 11.7 1.000 0.07 0.04 17.833 0.333 1,544.19 1.919E-06 518.9733 22.2671 539.67 545.23677 534.10323 0.00015 0.00009 0.00006
P11-P12 (WW Tanks) PF Resin - MeOH
0.17 10.5 35.0 17.5 Cone 1.0 22,669 22,669 80 10.40 529,151 2 264,575 MeOH 0.20%32.04 0.00527 <=Calc Antoine 1.06 0.68 3.48 7.897 1474.1 229.13 0.00527 11.7 1.000 1.06 0.68 17.833 0.333 1,544.19 2.915E-05 518.9733 22.2671 539.67 545.23677 534.10323 0.00617 0.00448 0.00169
P13-P17, P19-23, P25-
27 (RPPB;RPPD)PF Resin - HCHO 0.17 10.5 34.6
17.3
Cone 1.0 22,410 22,410 80 10.40 0 13 0 100% HCHO 0.20%30 0.00089 <=HCHO Eq.0.00 0.00 0.00 na na na 0.00089 0.0 1.000 0.00 0.11 17.633 0.333 1,526.88 4.599E-06 518.9733 22.2671 539.67 545.23677 534.10323 0.00112 0.00070 0.00041
P13-P17, P19-23, P25-
27 (RPPB;RPPD)PF Resin - Phenol 0.17 10.5 34.6
17.3
Cone 1.0 22,410 22,410 80 10.40 0 13 0 100% Phenol 0.20%94.1 0.00002 <=Calc Antoine 0.00 0.00 0.00 7.133 1516.8 174.95 0.00002 0.0 1.000 0.00 0.01 17.633 0.333 1,526.88 2.559E-07 518.9733 22.2671 539.67 545.23677 534.10323 0.00002 0.00001 0.00001
P13-P17, P19-23, P25-
27 (RPPB;RPPD)PF Resin - MeOH 0.17 10.5 34.6
17.3
Cone 1.0 22,410 22,410 80 10.40 0 13 0 100% MeOH 0.50%32.04 0.01317 <=Calc Antoine 0.00 0.00 0.00 7.897 1474.1 229.13 0.01317 0.0 1.000 0.00 1.67 17.633 0.333 1,526.88 7.287E-05 518.9733 22.2671 539.67 545.23677 534.10323 0.01543 0.01120 0.00424
S-1, S-8 (RPPI)PF Resin - HCHO 0.17 10.5 15.3 7.7 Cone 1.0 9,910 9,910 70 10.40 0 2 0 100% HCHO 9.40%30 0.00734 <=HCHO Eq.0.00 0.00 0.00 na na na 0.00734 0.0 1.000 0.00 0.41 7.983 0.333 691.28 3.874E-05 518.9733 22.2671 529.67 535.23677 524.10323 0.00930 0.00576 0.00354
S-1, S-8 (RPPI)PF Resin - Phenol 0.17 10.5 15.3 7.7 Cone 1.0 9,910 9,910 70 10.40 0 2 0 100% Phenol 0.60%94.1 0.00003 <=Calc Antoine 0.00 0.00 0.00 7.133 1516.8 174.95 0.00003 0.0 1.000 0.00 0.01 7.983 0.333 691.28 4.788E-07 518.9733 22.2671 529.67 535.23677 524.10323 0.00004 0.00002 0.00002
S-1, S-8 (RPPI)PF Resin - MeOH 0.17 10.5 15.3 7.7 Cone 1.0 9,910 9,910 70 10.40 0 2 0 100% MeOH 0.10%32.04 0.00196 <=Calc Antoine 0.00 0.00 0.00 7.897 1474.1 229.13 0.00196 0.0 1.000 0.00 0.12 7.983 0.333 691.28 1.106E-05 518.9733 22.2671 529.67 535.23677 524.10323 0.00232 0.00166 0.00066
S-3 (RPAB)PF Resin - HCHO 0.17 10.5 15.3 7.7 Cone 1.0 9,910 9,910 70 10.40 87,792 1 87,792 100% HCHO 3.00%30 0.00383 <=HCHO Eq.0.24 0.00 0.24 na na na 0.00383 8.9 1.000 0.24 0.21 7.983 0.333 691.28 2.019E-05 518.9733 22.2671 529.67 535.23677 524.10323 0.00485 0.00300 0.00184
S-3 (RPAB)PF Resin - Phenol 0.17 10.5 15.3 7.7 Cone 1.0 9,910 9,910 70 10.40 87,792 1 87,792 100% Phenol 14.90%94.1 0.00072 <=Calc Antoine 0.14 0.00 0.14 7.133 1516.8 174.95 0.00072 8.9 1.000 0.14 0.13 7.983 0.333 691.28 1.189E-05 518.9733 22.2671 529.67 535.23677 524.10323 0.00095 0.00054 0.00041
S-3 (RPAB)PF Resin - MeOH 0.17 10.5 15.3 7.7 Cone 1.0 9,910 9,910 70 10.40 87,792 1 87,792 100% MeOH 0.10%32.04 0.00196 <=Calc Antoine 0.13 0.00 0.13 7.897 1474.1 229.13 0.00196 8.9 1.000 0.13 0.12 7.983 0.333 691.28 1.106E-05 518.9733 22.2671 529.67 535.23677 524.10323 0.00232 0.00166 0.00066
S-2-4-5-9
(Alcohol Soluble)PF Resin - HCHO 0.17 10.5 15.3 7.7 Cone 1.0 9,910 9,910 70 9.40 34,362 4 8,590 100% .06 psi HCHO 1.00%30 0.00291 <=HCHO Eq.0.02 0.00 0.07 na na na 0.00291 0.9 1.000 0.02 0.15 7.983 0.333 691.28 1.537E-05 518.9733 22.2671 529.67 535.23677 524.10323 0.00369 0.00229 0.00140
S-2-4-5-9
(Alcohol Soluble)PF Resin - Phenol 0.17 10.5 15.3
7.7 Cone 1.0 9,910 9,910 70 9.40 34,362 4 8,590 100% .06 psi Phenol 11.00%94.1 0.00053 <=Calc Antoine 0.01 0.00 0.04 7.133 1516.8 174.95 0.00053 0.9 1.000 0.01 0.08 7.983 0.333 691.28 8.778E-06 518.9733 22.2671 529.67 535.23677 524.10323 0.00070 0.00040 0.00030
S-2-4-5-9
(Alcohol Soluble)PF Resin - MeOH 0.17 10.5 15.3 7.7 Cone 1.0 9,910 9,910 70 9.40 34,362 4 8,590 100% .06 psi MeOH 25.00%32.04 0.49055 <=Calc Antoine 3.21 0.00 12.86 7.897 1474.1 229.13 0.49055 0.9 1.000 3.21 28.61 7.983 0.333 691.28 0.0027652 518.9733 22.2671 529.67 535.23677 524.10323 0.57889 0.41398 0.16492
U1-U3
(Alcohol Soluble)PF Resin - HCHO 0.17 10.6 34.0
17.0 Cone 1.0 22,443 22,443 70 10.40 2,806,343 3 935,448 100% .06 psi HCHO 0.20%30 0.00058 <=HCHO Eq.0.34 0.00 1.03 na na na 0.00058 41.7 0.886 0.34 0.07 17.333 0.333 1,529.62 3.074E-06 518.9733 22.2671 529.67 535.23677 524.10323 0.00074 0.00046 0.00028
U1-U3
(Alcohol Soluble)PF Resin - Phenol 0.17 10.6 34.0 17.0 Cone 1.0 22,443 22,443 70 10.40 2,806,343 3 935,448 100% .06 psi Phenol 9.50%94.1 0.00046 <=Calc Antoine 0.85 0.00 2.55 7.133 1516.8 174.95 0.00046 41.7 0.886 0.85 0.16 17.333 0.333 1,529.62 7.581E-06 518.9733 22.2671 529.67 535.23677 524.10323 0.00060 0.00034 0.00026
U1-U3
(Alcohol Soluble)PF Resin - MeOH 0.17 10.6 34.0
17.0 Cone 1.0 22,443 22,443 70 10.40 2,806,343 3 935,448 100% .06 psi MeOH 18.00%32.04 0.35320 <=Calc Antoine 223.42 0.00 670.27 7.897 1474.1 229.13 0.35320 41.7 0.886 223.42 38.76 17.333 0.333 1,529.62 0.001991 518.9733 22.2671 529.67 535.23677 524.10323 0.41680 0.29806 0.11874
S-12 & S-22 PF Resin - HCHO 0.17 10.5 15.3 7.7 Cone 1.0 9,910 9,910 70 10.40 87,792 2 43,896 100% .06 psi HCHO 1.00%30 0.00291 <=HCHO Eq.0.09 0.00 0.18 na na na 0.00291 4.4 1.000 0.09 0.15 7.983 0.333 691.28 1.537E-05 518.9733 22.2671 529.67 535.23677 524.10323 0.00369 0.00229 0.00140
S-12 & S-22 PF Resin - Phenol 0.17 10.5 15.3 7.7 Cone 1.0 9,910 9,910 70 10.40 87,792 2 43,896 100% .06 psi Phenol 11.00%94.1 0.00053 <=Calc Antoine 0.05 0.00 0.10 7.133 1516.8 174.95 0.00053 4.4 1.000 0.05 0.08 7.983 0.333 691.28 8.778E-06 518.9733 22.2671 529.67 535.23677 524.10323 0.00070 0.00040 0.00030
S-12 & S-22 PF Resin - MeOH 0.17 10.5 15.3 7.7 Cone 1.0 9,910 9,910 70 10.40 87,792 2 43,896 100% .06 psi MeOH 7.00%32.04 0.13736 <=Calc Antoine 4.60 0.00 9.20 7.897 1474.1 229.13 0.13736 4.4 1.000 4.60 7.58 7.983 0.333 691.28 0.0007743 518.9733 22.2671 529.67 535.23677 524.10323 0.16209 0.11591 0.04618
S14-S17 & S21 Process Washwater - HCHO 0.17 10.5 15.3 7.7 Cone 1.0 9,910 9,910 75 10.40 1,852,027 5 370,405 HCHO 0.20%30 0.00072 <=HCHO Eq.0.18 0.04 1.12 na na na 0.00072 37.4 0.969 0.18 0.04 7.983 0.333 691.28 3.767E-06 518.9733 22.2671 534.67 540.23677 529.10323 0.00091 0.00057 0.00034
S14-S17 & S21 Process Washwater - Phenol 0.17 10.5 15.3 7.7 Cone 1.0 9,910 9,910 75 10.40 1,852,027 5 370,405 Phenol 1.50%94.1 0.00009 <=Calc Antoine 0.07 0.02 0.45 7.133 1516.8 174.95 0.00009 37.4 0.969 0.07 0.02 7.983 0.333 691.28 1.521E-06 518.9733 22.2671 534.67 540.23677 529.10323 0.00012 0.00007 0.00005
S14-S17 & S21 Process Washwater - MeOH 0.17 10.5 15.3 7.7 Cone 1.0 9,910 9,910 75 10.40 1,852,027 5 370,405 MeOH 0.20%32.04 0.00455 <=Calc Antoine 1.25 0.27 7.57 7.897 1474.1 229.13 0.00455 37.4 0.969 1.25 0.27 7.983 0.333 691.28 2.543E-05 518.9733 22.2671 534.67 540.23677 529.10323 0.00536 0.00386 0.00150
S20 (K-5 Distillate
Accumulation Tank)Distillate (< 0.5% HCHO)0.17 10.5 15.3 7.7 Cone 1.0 9,910 9,910 45 8.50 35,746 1 35,746 100% HCHO 0.50%30 0.00047 <=HCHO Eq.0.01 0.00 0.01 na na na 0.00047 3.6 1.000 0.01 0.03 7.983 0.333 691.28 2.612E-06 518.9733 22.2671 504.67 510.23677 499.10323 0.00061 0.00036 0.00025
S20 (K-5 Distillate
Accumulation Tank)Distillate (< 0.1% MeOH)0.17 10.5 15.3
7.7
Cone 1.0 9,910 9,910 45 8.50 35,746 1 35,746 100% MeOH 0.10%32.04 0.00088 <=Calc Antoine 0.02 0.00 0.02 7.897 1474.1 229.13 0.00088 3.6 1.000 0.02 0.06 7.983 0.333 691.28 5.232E-06 518.9733 22.2671 504.67 510.23677 499.10323 0.00106 0.00073 0.00033
S20 (K-5 Distillate
Accumulation Tank)Distillate (< 15% Phenol)0.17 10.5 15.3 7.7 Cone 1.0 9,910 9,910 45 8.50 35,746 1 35,746 100% Phenol 15.00%94.1 0.00019 <=Calc Antoine 0.01 0.00 0.01 7.133 1516.8 174.95 0.00019 3.6 1.000 0.01 0.04 7.983 0.333 691.28 3.231E-06 518.9733 22.2671 504.67 510.23677 499.10323 0.00026 0.00013 0.00012
S20 (K-5 Distillate
Accumulation Tank)Distillate (< 5% Cresols)0.17 10.5 15.3
7.7 Cone 1.0 9,910 9,910 45 8.50 35,746 1 35,746 100% Cresols (Mixed) 5.00%108.1 0.00300 <=Enter vp 0.28 0.00 0.28 N/A N/A N/A 0.00000 3.6 1.000 0.28 0.77 7.983 0.333 691.28 5.988E-05 518.9733 22.2671 504.67 510.23677 499.10323 Hand CalcHand Calc=>0.10000
<=Hand Enter!
S20 (K-5 Distillate
Accumulation Tank)Distillate (< 0.2% MEK)0.17 10.5 15.3 7.7 Cone 1.0 9,910 9,910 45 8.50 35,746 1 35,746 100% MEK 0.20%72.12 0.00139 <=Enter vp 0.09 0.00 0.09 N/A N/A N/A 0.00000 3.6 1.000 0.09 0.24 7.983 0.333 691.28 1.85E-05 518.9733 22.2671 504.67 510.23677 499.10323 Hand CalcHand Calc=>0.10000
<=Hand Enter!
S20 (K-5 Distillate
Accumulation Tank)Distillate (< 0.1% N-Butanol)0.17 10.5 15.3
7.7
Cone 1.0 9,910 9,910 45 8.50 35,746 1 35,746 100% N-Butanol 0.01%74.122 0.00011 <=Enter vp 0.01 0.00 0.01 N/A N/A N/A 0.00000 3.6 1.000 0.01 0.02 7.983 0.333 691.28 1.506E-06 518.9733 22.2671 504.67 510.23677 499.10323 Hand CalcHand Calc=>0.10000
<=Hand Enter!
K-5 Distillate Tank Distillate (< 0.5% HCHO)0.17 8 8.0 4.0 Cone 1.0 3,008 3,008 84 8.50 35,746 1 35,746 HCHO 0.50%30 0.00262 <=HCHO Eq.0.07 0.04 0.11 na na na 0.00262 11.9 1.000 0.07 0.04 4.333 0.333 217.82 1.345E-05 518.9733 22.2671 543.67 549.23677 538.10323 0.00327 0.00208 0.00120
K-5 Distillate Tank Distillate (< 0.1% MeOH)0.17 8 8.0 4.0 Cone 1.0 3,008 3,008 84 8.50 35,746 1 35,746 MeOH 0.10%32.04 0.00295 <=Calc Antoine 0.08 0.05 0.13 7.897 1474.1 229.13 0.00295 11.9 1.000 0.08 0.05 4.333 0.333 217.82 1.622E-05 518.9733 22.2671 543.67 549.23677 538.10323 0.00345 0.00252 0.00093
K-5 Distillate Tank Distillate (< 15% Phenol)0.17 8 8.0 4.0 Cone 1.0 3,008 3,008 84 8.50 35,746 1 35,746 Phenol 15.00%94.1 0.00143 <=Calc Antoine 0.11 0.08 0.19 7.133 1516.8 174.95 0.00143 11.9 1.000 0.11 0.08 4.333 0.333 217.82 2.301E-05 518.9733 22.2671 543.67 549.23677 538.10323 0.00184 0.00110 0.00075
K-5 Distillate Tank Distillate (< 5% Cresols)0.17 8 8.0 4.0 Cone 1.0 3,008 3,008 84 8.50 35,746 1 35,746 Cresols (Mixed) 5.00%108.1 0.00650 <=Enter vp 0.60 0.46 1.06 N/A N/A N/A 0.00000 11.9 1.000 0.60 0.46 4.333 0.333 217.82 0.0001204 518.9733 22.2671 543.67 549.23677 538.10323 Hand CalcHand Calc=>0.10000 <=Hand Enter!
K-5 Distillate Tank Distillate (< 0.1% MEK)0.17 8 8.0 4.0 Cone 1.0 3,008 3,008 84 8.50 35,746 1 35,746 MEK 0.10%72.12 0.00210 <=Enter vp 0.13 0.10 0.23 N/A N/A N/A 0.00000 11.9 1.000 0.13 0.10 4.333 0.333 217.82 2.59E-05 518.9733 22.2671 543.67 549.23677 538.10323 Hand CalcHand Calc=>0.10000 <=Hand Enter!
K-5 Distillate Tank Distillate (< 0.4% N-Butanol)0.17 8 8.0 4.0 Cone 1.0 3,008 3,008 84 8.50 35,746 1 35,746 N-Butanol 0.40%74.122 0.00067 <=Enter vp 0.04 0.03 0.07 N/A N/A N/A 0.00000 11.9 1.000 0.04 0.03 4.333 0.333 217.82 8.512E-06 518.9733 22.2671 543.67 549.23677 538.10323 Hand CalcHand Calc=>0.10000 <=Hand Enter!
MEK Tank (A-1)MEK 0.17 10.5 15.3 7.7 Cone 1.0 9,929 9,929 Amb 6.72 19,851 1 19,851 100% 98% MEK 100.00%72.12 1.08840 <=Enter vp 0.74 0.00 0.74 N/A N/A N/A 0.00000 2.0 1.000 37.10 776.21 7.998 0.333 692.58 0.0140444 518.9733 22.2671 520.835 526.40218 515.26864 Hand CalcHand Calc=>3.72000 <=Hand Enter!
U-5, U-7, U-9
(RUSR)UF Resin - HCHO 0.17 10.6 34.0
17.0 Cone 1.0 22,443 22,443 70 10.40 2,313,438 3 771,146 100% HCHO 1.00%30 0.00291 <=HCHO Eq.1.60 0.00 4.81 na na na 0.00291 34.4 1.000 1.60 0.36 17.333 0.333 1,529.62 1.537E-05 518.9733 22.2671 529.67 535.23677 524.10323 0.00369 0.00229 0.00140
U-5, U-7, U-9
(RUSR)UF Resin - MeOH 0.17 10.6 34.0 17.0 Cone 1.0 22,443 22,443 70 10.40 2,313,438 3 771,146 100% MeOH 0.40%32.04 0.00785 <=Calc Antoine 4.62 0.00 13.85 7.897 1474.1 229.13 0.00785 34.4 1.000 4.62 1.04 17.333 0.333 1,529.62 4.424E-05 518.9733 22.2671 529.67 535.23677 524.10323 0.00926 0.00662 0.00264
U-4 (WW) Process Washwater - HCHO
0.17 10.6 34.0
17.0
Cone 1.0 22,443 22,443 70 10.40 264,575 1 264,575 HCHO 0.20%30 0.00058 <=HCHO Eq.0.11 0.07 0.18 na na na 0.00058 11.8 1.000 0.11 0.07 17.333 0.333 1,529.62 3.074E-06 518.9733 22.2671 529.67 535.23677 524.10323 0.00074 0.00046 0.00028
U-4 (WW)Process Washwater - Phenol 0.17 10.6 34.0 17.0 Cone 1.0 22,443 22,443 70 10.40 264,575 1 264,575 Phenol 1.50%94.1 0.00007 <=Calc Antoine 0.04 0.03 0.07 7.133 1516.8 174.95 0.00007 11.8 1.000 0.04 0.03 17.333 0.333 1,529.62 1.197E-06 518.9733 22.2671 529.67 535.23677 524.10323 0.00010 0.00005 0.00004
U-4 (WW) Process Washwater - MeOH
0.17 10.6 34.0
17.0 Cone 1.0 22,443 22,443 70 10.40 264,575 1 264,575 MeOH 0.20%32.04 0.00392 <=Calc Antoine 0.79 0.52 1.31 7.897 1474.1 229.13 0.00392 11.8 1.000 0.79 0.52 17.333 0.333 1,529.62 2.212E-05 518.9733 22.2671 529.67 535.23677 524.10323 0.00463 0.00331 0.00132
U-6 (WW) Process Washwater - HCHO 0.17 12 32.5 16.3 Cone 1.0 27,494 27,494 70 10.40 264,575 1 264,575 HCHO 0.20%30 0.00058 <=HCHO Eq.0.11 0.09 0.20 na na na 0.00058 9.6 1.000 0.11 0.09 16.583 0.333 1,875.54 3.074E-06 518.9733 22.2671 529.67 535.23677 524.10323 0.00074 0.00046 0.00028
U-6 (WW)Process Washwater - Phenol 0.17 12 32.5 16.3 Cone 1.0 27,494 27,494 70 10.40 264,575 1 264,575 Phenol 1.50%94.1 0.00007 <=Calc Antoine 0.04 0.03 0.08 7.133 1516.8 174.95 0.00007 9.6 1.000 0.04 0.03 16.583 0.333 1,875.54 1.197E-06 518.9733 22.2671 529.67 535.23677 524.10323 0.00010 0.00005 0.00004
U-6 (WW) Process Washwater - MeOH
0.17 12 32.5 16.3 Cone 1.0 27,494 27,494 70 10.40 264,575 1 264,575 MeOH 0.20%32.04 0.00392 <=Calc Antoine 0.79 0.64 1.43 7.897 1474.1 229.13 0.00392 9.6 1.000 0.79 0.64 16.583 0.333 1,875.54 2.212E-05 518.9733 22.2671 529.67 535.23677 524.10323 0.00463 0.00331 0.00132
U-8, U-10
(RUSR)UF Resin - HCHO 0.17 12 32.5
16.3
Cone 1.0 27,494 27,494 70 10.40 1,542,292 3 514,097 100% HCHO 1.00%30 0.00291 <=HCHO Eq.1.07 0.00 3.21 na na na 0.00291 18.7 1.000 1.07 0.44 16.583 0.333 1,875.54 1.537E-05 518.9733 22.2671 529.67 535.23677 524.10323 0.00369 0.00229 0.00140
U-8, U-10
(RUSR)UF Resin - MeOH 0.17 12 32.5
16.3 Cone 1.0 27,494 27,494 70 10.40 1,542,292 3 514,097 100% MeOH 0.40%32.04 0.00785 <=Calc Antoine 3.08 0.00 9.23 7.897 1474.1 229.13 0.00785 18.7 1.000 3.08 1.27 16.583 0.333 1,875.54 4.424E-05 518.9733 22.2671 529.67 535.23677 524.10323 0.00926 0.00662 0.00264
Phenol = 2.5%0.17 10.5 35.0 17.5 Cone 1.0 22,669 22,669 Amb 8.66 43,096 1 4,975 Phenol 2.50%94.1 0.00008 <=Calc Antoine 0.00 0.03 0.03 7.133 1516.8 174.95 0.00008 0.2 1.000 0.00 0.03 17.833 0.333 1,544.19 1.284E-06 518.9733 22.2671 520.835 526.40218 515.26864 0.00010 0.00006 0.00005
Catechol = 0.5%0.17 10.5 35.0 17.5 Cone 1.0 22,669 22,669 Amb 8.66 43,096 1 4,975 Catechol 0.50%110.11 0.00058 <=Enter vp 0.01 0.32 0.33 N/A N/A N/A 0.00000 0.2 1.000 0.01 0.32 17.833 0.333 1,544.19 1.143E-05 518.9733 22.2671 520.835 526.40218 515.26864 Hand CalcHand Calc=>0.10000
Cresols (Mixed) = 85% (MAX)0.17 10.5 35.0 17.5 Cone 1.0 22,669 22,669 Amb 8.66 43,096 1 4,975 Cresols (Mixed) 85.00%108.1 0.007 <=Enter vp 0.09 3.76 3.85 N/A N/A N/A 0.00000 0.2 1.000 0.09 3.76 17.833 0.333 1,544.19 0.0001354 518.9733 22.2671 520.835 526.40218 515.26864 Hand CalcHand Calc=>0.10000
Naphthalene = 1%0.17 10.5 35.0 17.5 Cone 1.0 22,669 22,669 Amb 8.66 43,096 1 4,975 Naphthalene 1.00%128.17 0.00159 <=Enter vp 0.02 1.02 1.04 N/A N/A N/A 0.00000 0.2 1.000 0.02 1.02 17.833 0.333 1,544.19 3.636E-05 518.9733 22.2671 520.835 526.40218 515.26864 Hand CalcHand Calc=>0.10000
Formic Acid Storage 60% Formic 0.17 6 12.3 6.1 Cone 1.0 2,591 2,591 Amb 10.18 725 1 725 Formic 60.00%46 0.32292 <=Calc Antoine 0.26 7.97 8.22 7.581 1699.2 260.7 0.32292 0.3 1.000 0.26 7.97 6.458 0.333 182.61 0.0026577 518.9733 22.2671 520.835 526.40218 515.26864 0.37746 0.27528 0.10218
Acid Quench A 60% Formic 0.17 6 10.0 5.0 Cone 1.0 2,115 2,115 Amb 10.18 1 0 100% Formic 60.00%46 0.32292 <=Calc Antoine 0.00 0.00 0.00 7.581 1699.2 260.7 0.32292 0.0 1.000 0.00 6.69 5.333 0.333 150.80 0.0026577 518.9733 22.2671 520.835 526.40218 515.26864 0.37746 0.27528 0.10218
Acid Quench B 60% Formic 0.17 7 12.0 6.0 Cone 1.5 3,454 3,454 Amb 10.18 1 0 100% Formic 60.00%46 0.32292 <=Calc Antoine 0.00 0.00 0.00 7.581 1699.2 260.7 0.32292 0.0 1.000 0.00 10.91 6.500 0.500 250.15 0.0026577 518.9733 22.2671 520.835 526.40218 515.26864 0.37746 0.27528 0.10218
0 0.00000 <=Enter vp 0.00 0.00 0.00 N/A N/A N/A 0.00000 0.0 1.000 0.00 0.00 0.000 0.000 0.00 0 517.9533 15.6360 459.67 463.57901 455.76099 Hand CalcHand Calc=>0.10000
If not controlled temperature enter Amb.
Enter the pressure difference between the positive pressure setting and vacuum setting (e.g. .03 - (-.03) = .06)
Hand Calculated vp's (psi) Control of Working losses. Vapor returns typically assume 98% efficiency for working/filling losses.
HCHO 53.5 lb/yr Ammonia Ammonia Cresol Control of Breathing and Working losses. If controlled by oxidizer, assume 100% (emissions are already accounted for at oxidizer).
MeOH 880.3 lb/yr MW =17.03 17.03 Contorl of Breathing Losses. Tanks with a controlled temperature =100% .
Phenol 1,007.2 lb/yr Percentage =28%1%
Ammonia 278.7 lb/yr Temp (F) =
Formic 8.2 lb/yr Temp (F) =
Cresols (Mixed)5.2 lb/yr Temp (F) =
Cresols (m) 1.7 lb/yr Temp (F) =
Cresols (o).9 lb/yr Temp (F) = 95 0.308
Cresols (p)1.3 lb/yr Temp (F) =
Catechol .3 lb/yr Average Maximum Temp. (Tlx) (F) = 55.566771 12.14 <== Temperatures taken from Ammonia tank, which is under ambient conditions.
Naphthalene 1. lb/yr Average Annual Temp (Tla) (F) = 50 10.4 <== Ammonia Solution VP's from GPRI_Vapor Pressures
EPI . lb/yr Average Minimum Temp. (Tln) (F) = 44.4 8.42
MEK 1.1 lb/yr Temp (F) = 50 6.63
N-Butanol .1 lb/yr
Check: OK dPv = (Tlx-Tln) = 3.72 n/a n/a n/a n/a n/a Comments for Tanks Calculations
Table 7.1-6 Paint Factor Table 7.1-5 Vapor Pressure Equation Constants
Paint Factor Based on Celsius
Paint Condition A B C MW Density
Paint Color Shade Good Poor HCHO Special Equation (based on K)30 9.5
Aluminum Specular 0.39 0.49 MeOH 7.897 1474.08 229.13 32.04 6.63
Aluminum Diffuse 0.6 0.68 Phenol 7.133 1516.79 174.95 94.1 8.92
Gray Light 0.54 0.63 Formic 7.581 1699.2 260.7 46.0 10.18
Gray Medium 0.68 0.74 EPI 8.2294 2086.806 273.16 92.5 9.848
Red Primer 0.89 0.91 Acetone 7.117 1210.595 229.664 58.08 6.628
White NA 0.17 0.34
(1) If Roof and Shell are different, factor = average.
(2) Assume White and Good Condition if specific
Information is not available.
Raleigh, North Carolina
1) For consistency, forced usage is used for tanks throughputs rather and receipts.
3) Acid quench tanks are pressurized and have no emissions.
7) 2009RY: Remeoved MSBP from 2008 switch to CTP.
5) 4/30/07: Changed CA83 tank to MSBP tank with 0.3% Phenol & remainder VOC.
4) The CA83BL Tank has zero Cresols. The throughput for the CA41 & CA44 is used for this tank to simulate the emissions from the drums and/or totes of CA41 & CA44.
6) 2008RY: Changed Cresylic tank to Cresylic CTP with cresols
Tank Emissions Summary (Section 5.2)
R-3
Cresylic Acid (CTP)
2) HCHO and MeOH Tanks are controlled by oxidizer. Emissions are captured in those calculations.
10) The following are NOT stored in bulk: Styrene, N-Butanol, MIBK, CA41
8) Converted S-20 tank to K-5 Distillate Accumulation Tank
9) Added K-5 Distillate Tank
12) 2011RY: Changed service of C(1-3) to non VOC / Form R chemicals
11) 2011RY: Ajusted use of all tanks (minor tweaks)
12) 2011RY: Accounting for all (16) WW tanks.
11) 2011RY: Added Recycle logic for methanol/HCHO tanks as well as ammonia scrubber.
Antoine's Constants
This is a controlled document.
https://thebakelite.sharepoint.com/sites/GP_BPEnvDocuments/NC090_DL/01 Air/Reports/AEI/Emissions Inventory/2021RY/04 - Calculation Spreadsheet - Final/CON_2021RY_EI_SARA 313_Calcs_FINAL
Tanks
Tanks Page 1
.
HCHO Plant(s)
Reporting Year 7,992 <==Calculaed Production Hours based on 23gpm methanol feedrate
Location 8,446 <==2021RY Actual run time
Emissions from RCI Formaldehyde Plant:
DT Hours 313.97
Con- 50% Oxidizer Oxidizer Uncontrolled Annual Prod. Treated Oxidizer Total
MeOH version HCHO Inlet Outlet DRE Emiss. Rate (50% HCHO Onsite Emiss.Emiss.
Plant Pollutant (gpm)Ratio (tons/hr)(lb/hr)(lb/hr)(%)(lbs/ton) & UFC) (tpy)(lbs/yr)(lbs/yr)(lbs/yr)
Methanol 23.0 11.28 7.783 19.97 0.320 98.4%2.57 62,201 157,037 2,557 2,558 0.52 90%1.0 1.0 0.1 5.7 6.8 21.6
Formaldehyde 23.0 11.28 7.783 18.70 0.380 98.0%2.40 62,201 146,408 3,037 3,038 0.00 75%0.0 0.0 0.0 0.0 0.0 0.0
Acetaldehyde 23.0 11.28 7.783 2.87 0.0025 99.9% 0.37
62,201 22,916 20 20.13 0.0 0.0 0.0 0.0 0.0 0.0
DME 23.0 11.28 7.783 109.87 2.230 98.0% 14.12
62,201 860,229 17,822 17,827 0.0 0.0 0.0 0.0 0.0 0.0
VOC 23.0 11.28 7.783 131.44 2.61 98.0% 16.89
62,201 1,029,554 20,878 20,885 0.0 0.0 0.0 0.0 0.0 0.0
CO 23.0 11.28 7.783 415.46 1.140 99.7% 53.38 62,201 3,311,132 9,111 9,132 0.0 0.0 0.0 0.0 0.0 0.0
Total 1 1 0 6 7 22
NOTE: The Conway RCI process is interlocked to prevent bypass of HCHO Plant.
24,240.11
168.00 Resin Plant
226 Spray Dryer
24,634.11
VOC CO
RCI
Plant
<== Short flameout with minor low delta T
<== Longer flameouts with low delta T
<== Other
<== Other
Annual
Excess
Emissions
(Hours)
%
DRE HCHOMeOH Acetalde
hyde DME
<== Other
<== Other
Annual Emissions from Bypasses in (lbs):
2021RY
Conway, NC
Catalytic Oxidizer Stack Test dated: 4/26/2016 Current Production and Emissions
Georgia-Pacific Resins 2 CON_2021RY_EI_SARA 313_Calcs_FINAL
Resin Plant
Reporting Year TO Annual Downtime Hours =42.57
Location
Emissions from Resin Process
Oxidizer # of Kettles
Uncontrolled
Emission Oxidizer Destruction Resin Prod. Emission
Inlet Contributing to Factor Outlet Efficiency during test Factor
Pollutant (lbs/hr) to Emissions (lbs / kettle hr) (lbs/hr) DRE (%) (lbs/ kettle hr)
(lbs / ton
Resin)
MeOH 2.58 4 0.65 0.041 98.4% 13,737 0.0939
HCHO 0.1 4 0.03 0.004 96.0% 13,737 0.0036
Phenol 0.01 3 0.003 0.004 98.4% 14,796 0.0005 <==Calculated ND values calculated as MDL * 50%
Acetaldehyde 0.03 4 0.008 0.002 98.4%13,737 0.0011 <==Calculated ND values calculated as MDL * 50%
N-Butanol 0.0025 1 0.003 0.0035 98.4% 1,555 0.0032 <==Calculated ND values calculated as MDL * 50%
Styrene 0.002 1 0.002 0.0025 98.4% 1,732 0.0023 <==Calculated ND values calculated as MDL * 50%
DEA 0.003 1 0.003 0.004 98.4% 12,987 0.0005 <==Calculated ND values calculated as MDL * 50%
MIBK 0.0025 1 0.003 0.003 98.4% 0 0.0000 <==Calculated ND values calculated as MDL * 50%
MEK 0.0015 1 0.002 0.002 98.4% 1,346 0.0022 <==Calculated ND values calculated as MDL * 50%
m-Cresol 0.0025 1 0.003 0.0035 98.4% 0 0.0000 <==Calculated ND values calculated as MDL * 50%
o-Cresol 0.0025 1 0.003 0.0035 98.4% 1,585 0.0032 <==Calculated ND values calculated as MDL * 50%
p-Cresol 0.003 1 0.003 0.004 98.4% 0 0.0000 <==Calculated ND values calculated as MDL * 50%
Cresols (Mixed Isomers) 0.008 1 0.008 0.011 98.4% 15,183 0.0011 <==Calculated ND values calculated as MDL * 50%
DME (VOC)0.71 4 0.18 0.009 98.7% 13,737 0.0258
Total HAPs 50%MDL 2.74 4 0.68 0.077 97.2%13,737 0.0997 <==Calculated with MDL * 50%
Total VOCs 50%MDL 3.45 4 0.86 0.086 97.5%13,737 0.1256 <==Calculated with MDL * 50%
Total HAPs 2.72 4 0.68 0.045 98.3% 13,737 0.0990 <==Calculated withOUT MDL * 50%
Total VOCs 3.43 4 0.86 0.054 98.4%13,737 0.1248 <==Calculated withOUT MDL * 50%. This Method 320 VOC DRE which is believed to me most representative should be used as DRE for compounds which were non detect.
Total VOCs M25A as MeOH 3.36 4 0.84 0.10 97.0%13,737 0.1223 <==Method 25A destruction efficiency (DRE) should be used in lieu of DRE with trace detection amounts
NOx --- 0.00 0.21 0.0% 13,737 0.0306 <==Outlet values used vs. inlet because more impacted from combusion vs process.
CO 0.001 0.00 0.96 0.0% 13,737 0.1398 <==Outlet values used vs. inlet because more impacted from combusion vs process.
Ammonia 0.013 3 0.004 0.004 69.2%13,737 0.0019 <==DRE is actually greater than calculated because ammonia is formed in combustion of VOCs and natural gas.
Kettle Numbers K(1,3,5,7)K(2,8)Total
Product Type / Chemical PF UF N-Butanol Styrene DEA MIBK MEK Cresols - O Cresols - Mixed
Annual Production (lbs)284,198,506 40,099,600 769,100 195,880 0 0 557,100 259,250 20,735,508 324,298,106 <==Because all chemical compounds in column D-J are also UF or PF Resins, they around not included in Resin Total
Annual Production (Tons)142,099 20,050 385 98 0 0 279 130 10,368 162,149 <==Because all chemical compounds in column D-J are also UF or PF Resins, they around not included in Resin Total
Total Kettle (Hrs) 19,393 2,895 598.3 146.2 0.0 0.0 399.6 133.1 1,069.1 22,288 <==Because all chemical compounds in column D-J are also UF or PF Resins, the hours of opoeration is not included in Resin Total
Prod. Rate (tons/hr)7.33 6.93 0.64 0.67 0.00 0.00 0.70 0.97 9.70 7.28
Event
Event
Minutes
Number
of
Reactors PF/UF/Boils PF/Boils N-Butanol Styrene DEA MIBK MEK Cresols - O Cresols - Mixed
MeOH 162,149 14,985 242 MeOH 22,288 14,147 228
4 0.0 228 01/11/21 0 0 0 0
HCHO 162,149 567 24 HCHO 22,288 535 22
4 0.0 22 03/27/21 0 0 0 0
Phenol 142,099 63 1 Phenol 19,393 64 1
2 0.0 1.0 04/28/21 0 0 0 0
Acetaldehyde 162,149 174 3 Acetaldehyde 22,288 165 3
4 0.0 2.63 06/03/21 0 0 0 0
N-Butanol 385 1 0 N-Butanol 598 1.5 0.024
0 0.0 0.02 07/08/21 0 0 0 0
Styrene 98 0 0 Styrene 146 0.3 0
0 0.0 0.005 09/02/21 0 0 0 0
DEA 0 0 0 DEA 0 0.0 0
0 0.0 0.000 11/04/21 2 2 2 1
MIBK 0 0 0 MIBK 0 0.0 0
0 0.0 0.000 11/11/21 0 0 0 0
MEK 279 1 0 MEK 400 0.6 0
0 0.0 0.009 11/11/21 0 0 0 0
m-Cresol 10,368 0 0 m-Cresol 1,069 2.6 0
0 0.0 0.042 12/28/21 0 0 0 0
o-Cresol 130 0.4 0.0 o-Cresol 133 0.3 0
0 0.0 0.005 12/29/21 0 0 0 0
p-Cresol 10,368 0 0 p-Cresol 1,069 3.2 0
0 0.0 0.050
Cresols (Mixed Isomers)10,368 11 0 Cresols (Mixed Isomers)1,069 8.4 0.1 0 0.0 0.13
DME (VOC)162,149 4,137 53 DME (VOC)22,288 3,906 50 4 0.0 50.2
Total HAPs 162,149 15,713 454 Total HAPs 22,288 14,835 429 0.0 429.0
Total VOCs 162,149 19,851 508 Total VOCs 22,288 18,741 479 0.0 479.2
4 2 - - - - - - -
Total HAPs 162,149 15,787 266 Total HAPs 22,288 14,905 251 0.0 250.7
Total VOCs 162,149 19,924 319 Total VOCs 22,288 18,811 301 0.0 300.9
NOx 0 0 0 NOx 8,717 0 1,831 0 0.0 1,831
CO 0 0 0 CO 8,717 0 8,369 0 0.0 8,369
Ammonia 0 0 0 Ammonia 8,717 37 35 4 0.0 35
2021RY
Conway, NC
Thermal Oxidizer Stack Test dated 4/26/16
Kettle Production Data for current Reporting Year
Oxidizer
Emissions
(lbs/yr)
Kettles (Specialty Chemicals)
Reactor Bypasses
(Reactor Minutes)
Bypass
Emissions
(lbs)
TOTAL Emissions
(lbs)
Production
Basis (Hrs)
Emissions using (lb/ton) Emission Factor Emissions using (lb/hr) Emission Factor using "Actual" kettle hours Annual Emissions (lbs)
Pollutant Production
Basis (tons)
Treated Onsite
(lbs/yr)
Oxidizer
Emissions (lbs/yr)Pollutant Treated Onsite
(lbs/yr)
2020 Bypass Events
Georgia-Pacific Resin CON_2021RY_EI_SARA 313_Calcs_FINAL
GPRI Environmental
Reporting Year 2021RY
Plant Location Conway, NC
Note: The ELDACs online database was used for equipment counts. A backup PDF of these reports is posted with the SARA calculations.
MeOH (LL) HCHO (HL) MeOH (LL) HCHO (HL) UFC (HL) Phenol (HL) Cresols (HL) MEK (LL) MIBK (LL) MeOH (LL) HCHO (HL) Phenol (HL) Cresols (HL) MEK (LL) MIBK (LL)
Emission LDAR Average Plant A 100% 50% 100% 50% 30% 100% 85% 100% 100% 100% 50% 100% 85% 100%100%
Factor Control Operating Hrs.
Equipment % of Counts % of Counts Equipment Equipment Equipment Equipment Equipment Equipment Equipment Equipment % of Counts % of Counts % of Counts % of Counts % of Counts % of Counts
Component Type (lb/hr/source) Efficiency (hr/yr) Counts in Stream in Stream Counts Counts Counts Counts Counts Counts Counts Counts Mixed Stream Mixed Stream Mixed Stream Mixed Stream Mixed Stream Mixed Stream
Agitators (LL/GV) 0.0386 0.93 8,760 0 0 0 0 0 0 0 0 13 60% 25% 11% 2% 2% 0%Sum = 100%
Agitators (HL) 0.0161 0.93 8,760 0 0 0 0 0 0 0 0 0 0% 0% 0% 0% 0% 0%Check Percentages
Closed Vent Systems
Connectors (LL) 0.0005 0.75 8,760 210 100% 0% 80 0 0 0 0 110 0 357 15% 40% 40% 5% 0% 0%Sum = 100%
Connectors (GV) 0.0029 0.75 8,760 76 64% 36% 41 0 0 21 0 0 0 365 60% 25% 13% 2% 0% 0%Sum = 100%
Connectors (HL) 0.00007 0.75 8,760 373 0% 100% 69 0 50 250 58 0 0 519 57% 25% 10% 5% 3% 0%Sum = 100%
End Caps for Open Ended Lines
Group Tag
Instrumentation Systems (LL) 0.0005 0.75 8,760 0 100% 0
Instrumentation Systems (GV) 0.0029 0.75 8,760 0 50% 50% 0
Instrumentation Systems (HL) 0.00007 0.75 8,760 0 100% 0
Other (LL) 0.0005 0.75 8,760 0 100% 0
Other (GV) 0.0029 0.75 8,760 0 50% 50% 0
Other (HL) 0.00007 0.75 8,760 0 100% 0
PRD (LL) 0.0005 0.75 8,760 1 100% 0
PRD (GV) 0.0029 0.75 8,760 5 100% 1 1 16 60% 25% 11% 2% 2% 0%Sum = 100%
PRD (HL) 0.00007 0.75 8,760 0 100% 0
Pumps (LL) 0.0386 0.93 8,760 3 100% 1 0 0 0 0 1 0 4 55% 10% 30% 5%Sum = 100%
Pumps (HL) 0.0161 0.93 8,760 3 100% 0 2 2 4 2 0 0 15 55% 10% 30% 5%Sum = 100%
Sampling System
Valves (LL) 0.0035 0.97 8,760 59 100% 30 0 0 0 0 32 0 93 20% 40% 40%Sum = 100%
Valves (GV) 0.0089 0.97 8,760 18 44% 56% 5 0 0 0 0 0 0 41 41% 27% 26% 3% 3% 0%Sum = 100%
Valves (HL) 0.0007 0.97 8,760 84 100% 13 62 19 80 23 0 0 134 25% 40% 25% 5% 5% 0%Sum = 100%
Misc & Other (LL) 0.0005 0.75 8,760 0 100%.
Misc & Other (GV) 0.0029 0.75 8,760 0 50% 50%
Misc & Other (HL) 0.00007 0.75 8,760 0 100%
Sub -total Emissions (lbs/yr) => 716 150 430 16 9 226 28 180 0 1,937 476 649 80 15 0
HCHO Plant Resin Plant
Chemical Emissions (lbs/yr)Emissions (lbs/yr) Emissions (lbs/yr)
Methanol 3,083
Formaldehyde 651 150 501
Phenol 875
Cresols (Mixed) 108
Cresols (m) 47
Cresols (o) 24
Cresols (p) 38
MEK 195
MIBK 0
Emissions
Factor(1)Control
Component Type (lb/hr/source)
Efficiency (%)(1)
Valves (GV) 0.0089 97%
Valves (LL) 0.0035 97%
Valves (HL) 0.0007 97%
Pumps (LL) & Agitators (GV/LL)0.0386 93%
Pumps (HL) & Agitators (HL)0.0161 93%
Connectors, PRD, Misc. (G/V)0.0029 75%
Connectors, PRD, Misc. (LL)0.0005 75%
Connetors, PRD, Misc. (HL)0.00007 75%
(1)Emission factors and control efficiencies are taken from the TNRCC "Technical Guidance for Chemical Sources Equipment Leak Fugitives" (March 1995).
Factors based on SOCMI without C2. See supporting guidance document for details.
Weekly audio/visual/olfactory inspections w/ leak repair. Note GPRI conducts weekly area inspections. Policy &
training also in place to repair any leak discovered during normal activities. Same efficiency as the annual
monitioring is appropriate.
28MID program (500 ppm leak definition & quarterly monitoring). Note GPRI repairs leaks >100 ppm.
28MID program (500 ppm leak definition & quarterly monitoring). Note GPRI repairs leaks >100 ppm.
Weekly audio/visual/olfactory inspections w/ leak repair. Note GPRI conducts weekly area inspections. Policy &
training also in place to repair any leak discovered during normal activities.
28MID program (500 ppm leak definition & quarterly monitoring). Note GPRI monitors monthly and repairs
leaks >100 ppm.
Weekly audio/visual/olfactory inspections w/ leak repair. Note GPRI conducts weekly area inspections. Policy &
training also in place to repair any leak discovered during normal activities.
Gas/Vapor and Light Liquid Connectors are monitored annually and are included in weekly walk around
inspections. While a greater efficiency could be justified, the lower 75% control factor was conservatively
selected to account for the areas that are les
Gas/Vapor and Light Liquid Connectors are monitored annually and are included in weekly walk around
inspections. While a greater efficiency could be justified, the lower 75% control factor was conservatively
selected to account for the areas that are les
Basis
GPRI Fugitive Emission Factors for LDAR Equipment Leaks:
Formaldehyde Plant(s)Individual Liquid LDAR Streams (Resin MACT)Mixed Streams (Resin MACT)
Template
Revision 1.1
02/16/2005 This "Template" is a controlled electronic document.
CON_2021RY_EI_SARA 313_Calcs_FINAL
LDAR
Template Owner:
Division Environmental
Manager
Tanker_DrumFilling
Reporting Year 2021RY
Location Conway, NC
Loading Rack & Drum/Tote Filling Emissions:
Note #1: Unless otherwise inputted, all "Resin" throughput is assumed to equal the forced production.
Throughput
(pounds)
Density
(lb/gal)
Throughput
(gallons) 59.2833 F = average ambient temperature for Raleigh, NC. Taken from TANKS Program
Resimix (RPMX / RPMM)115,756,430 10.00 11,575,643
Insulating Resins (RPPI)0 10.00 0
OSB (RPPB)92,172,956 10.20 9,036,564 Equation: For Tank Loading
Hardboard (RPPD)0 10.10 0 L = 12.46 x (S*pp*MW/T)
Abbrasives (RPAB)913,040 10.40 87,792 L = Loading loss, lb/1000 gal
Electrical Laminates (RPEL)323,000 9.35 34,545 S = Saturation Factor (AP42 Table 5.2-1, 01/95)
High Pressure Laminates (RPHP)29,185,963 9.60 3,040,204
RPPC 2112 Resin = 414,000 9.35 44,278 Note: S = 0.6 for "Submerged" filling & S = 1.45 for "non Submerged" filling
RPPC 2640 Resin = 259,250 8.34 31,085
RPPC 791C99 Resin = 144,450 8.92 16,194 Equation 11
OTHER (RPPC)1,018,293 8.84 115,192 E = mass emitted per fill
Saturating (RPPF)0 9.50 0 E = V/(R*T) x (pp)(MW)
Floral Foam (RPFM)0 10.85 0 Gas Constant (R) =10.73 ft3 x psia / lb-mole x ºR
Filter Resins (RPLS)1,170,519 10.35 113,094 Total Emissions = E x Throughput/Vessel Size
Impregnating Resins (RPMS)654,729 10.45 62,653 Note: This equation yields the same results as a Splash Factor of 1.0
Calculated "Other PF Resins (non-specialty resins)"0 10.45 0
Resorcinol Resin - "RR" Total 0 9.60 0 pp = Partial Pressure of Liquid, psia
UF / MUF Resin - "RU" Total 40,099,600 10.85 3,695,816 M = Molecular Weight of vapors
AF Resin (CORM)0 9.70 0 T = Temp of liquids, R (460 + F)
AF Resi Mix (COCM)0 10.42 0
MF Resin - "RM" Total 14,633 10.10 1,449
Total HCHO Shipped = 7,261,560 9.12 796,224
Total UFC Shipped = 0 10.40 0
Total Methanol Shipped = 0 6.63 0
Product Loaded
Throughput
(gal) S
Temp at Load
Condition
(F)
+5% OHAP
(Resin Affected
Source)
Chemical Percent of Free
Chemical MW
Control
Efficiency
(%)
Partial vp at
Storage
Condition
(psi)
Emission Factor
(lbs/1,000 gal)
Controlled
Emissions
(lbs)A B C
Calc. partial vapor
pressure (psi)
11,575,643 1.45 85.00 HCHO 0.10%30 0%0.00054 <=HCHO Eq.0.0005 6.27 na na na 0.00054
11,575,643 1.45 85.00 MeOH 0.00%32.04 0%0.00000 <=Calc Antoine 0.0000 0.00 7.897 1474.08 229.13 0.00000
11,575,643 1.45 85.00 Phenol 0.00%94.1 0%0.00000 <=Calc Antoine 0.0000 0.00 7.133 1516.79 174.95 0.00000
0 1.45 50.00 HCHO 9.00%30 0%0.00291 <=HCHO Eq.0.0031 0.00 na na na 0.00291
0 1.45 50.00 MeOH 0.00%32.04 0%0.00000 <=Calc Antoine 0.0000 0.00 7.897 1474.08 229.13 0.00000
0 1.45 50.00 Phenol 0.00%94.1 0%0.00000 <=Calc Antoine 0.0000 0.00 7.133 1516.79 174.95 0.00000
9,036,564 1.45 78.00 HCHO 0.20%30 0%0.00082 <=HCHO Eq.0.0008 7.44 na na na 0.00082
9,036,564 1.45 78.00 MeOH 0.00%32.04 0%0.00000 <=Calc Antoine 0.0000 0.00 7.897 1474.08 229.13 0.00000
9,036,564 1.45 78.00 Phenol 0.00%94.1 0%0.00000 <=Calc Antoine 0.0000 0.00 7.133 1516.79 174.95 0.00000
0 1.45 72.00 HCHO 0.20%30 0%0.00063 <=HCHO Eq.0.0006 0.00 na na na 0.00063
0 1.45 72.00 MeOH 0.00%32.04 0%0.00000 <=Calc Antoine 0.0000 0.00 7.897 1474.08 229.13 0.00000
0 1.45 72.00 Phenol 0.00%94.1 0%0.00000 <=Calc Antoine 0.0000 0.00 7.133 1516.79 174.95 0.00000
87,792 1.45 75.00 HCHO 0.80%30 0%0.00288 <=HCHO Eq.0.0029 0.26 na na na 0.00288
87,792 1.45 75.00 MeOH 0.00%32.04 0%0.00000 <=Calc Antoine 0.0000 0.00 7.897 1474.08 229.13 0.00000
87,792 1.45 75.00 Phenol 7.00%94.1 0%0.00043 <=Calc Antoine 0.0014 0.12 7.133 1516.79 174.95 0.00043
34,545 1.45 72.00 HCHO 1.00%30 0%0.00317 <=HCHO Eq.0.0032 0.11 na na na 0.00317
34,545 1.45 72.00 MeOH 25.00%32.04 0%0.52087 <=Calc Antoine 0.5668 19.58 7.897 1474.08 229.13 0.52087
34,545 1.45 72.00 Phenol 11.00%94.1 0%0.00059 <=Calc Antoine 0.0019 0.06 7.133 1516.79 174.95 0.00059
3,040,204 1.45 72.00 HCHO 0.20%30 0%0.00063 <=HCHO Eq.0.0006 1.96 na na na 0.00063
3,040,204 1.45 72.00 MeOH 18.00%32.04 0%0.37502 <=Calc Antoine 0.4081 1,240.59 7.897 1474.08 229.13 0.37502
3,040,204 1.45 72.00 Phenol 9.50%94.1 0%0.00051 <=Calc Antoine 0.0016 4.92 7.133 1516.79 174.95 0.00051
44,278 1.00 108 HCHO 1.00%30 100%0.01335 <=HCHO Eq.0.0088 0.00 na na na 0.01335
44,278 1.00 108 MeOH 0.00%32.04 100%0.00000 <=Calc Antoine 0.0000 0.00 7.897 1474.08 229.13 0.00000
44,278 1.00 108 Phenol 8.50%94.1 100%0.00231 <=Calc Antoine 0.0048 0.00 7.133 1516.79 174.95 0.00231
44,278 1.00 108 N-Butanol 0.00%74.12 98%0.00000 <=Enter vp 0.0000 0.00 N/A N/A N/A 0.00000
44,278 1.00 108 Cresols 0.00%108.1 100%0.00000 <=Enter vp 0.0000 0.00 N/A N/A N/A 0.00000
44,278 1.00 108 MEK 24.00%72.12 100%0.90461 <=Enter vp 1.4312 0.00 N/A N/A N/A 0.00000
31,085 1.00 104 HCHO 0.50%30 100%0.00574 <=HCHO Eq.0.0038 0.00 na na na 0.00574
31,085 1.00 104 MeOH 0.00%32.04 100%0.00000 <=Calc Antoine 0.0000 0.00 7.897 1474.08 229.13 0.00000
31,085 1.00 104 Phenol 7.50%94.1 100%0.00173 <=Calc Antoine 0.0036 0.00 7.133 1516.79 174.95 0.00173
31,085 1.00 104 N-Butanol 50.00%74.12 98%0.18274 <=Enter vp 0.2992 0.19 N/A N/A N/A 0.00000
31,085 1.00 104 Cresols 2.00%108.1 100%0.00032 <=Enter vp 0.0008 0.00 N/A N/A N/A 0.00000
31,085 1.00 104 MEK 0.00%72.12 100%0.00000 <=Enter vp 0.0000 0.00 N/A N/A N/A 0.00000
16,194 1.00 104 HCHO 0.80%30 100%0.00919 <=HCHO Eq.0.0061 0.00 na na na 0.00919
16,194 1.00 104 MeOH 0.00%32.04 100%0.00000 <=Calc Antoine 0.0000 0.00 7.897 1474.08 229.13 0.00000
16,194 1.00 104 Phenol 5.00%94.1 100%0.00115 <=Calc Antoine 0.0024 0.00 7.133 1516.79 174.95 0.00115
16,194 1.00 104 N-Butanol 45.00%74.12 98%0.16447 <=Enter vp 0.2693 0.09 N/A N/A N/A 0.00000
16,194 1.00 104 Cresols 0.00%108.1 100%0.00000 <=Enter vp 0.0000 0.00 N/A N/A N/A 0.00000
16,194 1.00 104 MEK 0.00%72.12 0%0.00000 <=Enter vp 0.0000 0.00 N/A N/A N/A 0.00000
115,192 1.00 65.00 HCHO 0.50%30 100%0.00117 <=HCHO Eq.0.0008 0.00 na na na 0.00117
115,192 1.00 65.00 MeOH 4.00%32.04 100%0.06740 <=Calc Antoine 0.0513 0.00 7.897 1474.08 229.13 0.06740
115,192 1.00 65.00 Phenol 7.50%94.1 100%0.00028 <=Calc Antoine 0.0006 0.00 7.133 1516.79 174.95 0.00028
0 1.45 75.00 HCHO 0.80%30 0%0.00288 <=HCHO Eq.0.0029 0.00 na na na 0.00288
0 1.45 75.00 MeOH 24.00%32.04 0%0.54655 <=Calc Antoine 0.5914 0.00 7.897 1474.08 229.13 0.54655
0 1.45 75.00 Phenol 4.50%94.1 0%0.00028 <=Calc Antoine 0.0009 0.00 7.133 1516.79 174.95 0.00028
0 1.45 62.00 HCHO 5.50%30 0%0.00361 <=HCHO Eq.0.0037 0.00 na na na 0.00361
0 1.45 62.00 MeOH 0.00%32.04 0%0.00000 <=Calc Antoine 0.0000 0.00 7.897 1474.08 229.13 0.00000
0 1.45 62.00 Phenol 3.70%94.1 0%0.00012 <=Calc Antoine 0.0004 0.00 7.133 1516.79 174.95 0.00012
113,094 1.45 70.00 HCHO 3.00%30 0%0.00383 <=HCHO Eq.0.0039 0.44 na na na 0.00383
113,094 1.45 70.00 MeOH 0.00%32.04 0%0.00000 <=Calc Antoine 0.0000 0.00 7.897 1474.08 229.13 0.00000
113,094 1.45 70.00 Phenol 14.90%94.1 0%0.00072 <=Calc Antoine 0.0023 0.26 7.133 1516.79 174.95 0.00072
62,653 1.00 75.00 HCHO 1.00%30 0%0.00360 <=HCHO Eq.0.0025 0.16 na na na 0.00360
62,653 1.00 75.00 MeOH 0.00%32.04 0%0.00000 <=Calc Antoine 0.0000 0.00 7.897 1474.08 229.13 0.00000
62,653 1.00 75.00 Phenol 12.50%94.1 0%0.00077 <=Calc Antoine 0.0017 0.11 7.133 1516.79 174.95 0.00077
0 1.45 50.00 HCHO 0.20%30 0%0.00024 <=HCHO Eq.0.0003 0.00 na na na 0.00024
0 1.45 50.00 MeOH 0.10%32.04 0%0.00104 <=Calc Antoine 0.0012 0.00 7.897 1474.08 229.13 0.00104
0 1.45 50.00 Phenol 0.20%94.1 0%0.00000 <=Calc Antoine 0.0000 0.00 7.133 1516.79 174.95 0.00000
0 1.45 75.00 HCHO 0.10%30 0%0.00036 <=HCHO Eq.0.0004 0.00 na na na 0.00036
0 1.45 75.00 MeOH 0.00%32.04 0%0.00000 <=Calc Antoine 0.0000 0.00 7.897 1474.08 229.13 0.00000
0 1.45 75.00 Phenol 10.00%94.1 0%0.00062 <=Calc Antoine 0.0020 0.00 7.133 1516.79 174.95 0.00062
3,695,816 1.45 75.00 HCHO 0.20%30 0%0.00072 <=HCHO Eq.0.0007 2.70 na na na 0.00072
3,695,816 1.45 75.00 MeOH 0.00%32.04 0%0.00000 <=Calc Antoine 0.0000 0.00 7.897 1474.08 229.13 0.00000
3,695,816 1.45 75.00 Phenol 0.00%94.1 0%0.00000 <=Calc Antoine 0.0000 0.00 7.133 1516.79 174.95 0.00000
0 1.45 75.00 HCHO 0.30%30 0%0.00108 <=HCHO Eq.0.0011 0.00 na na na 0.00108
0 1.45 75.00 MeOH 0.00%32.04 0%0.00000 <=Calc Antoine 0.0000 0.00 7.897 1474.08 229.13 0.00000
0 1.45 75.00 Phenol 0.00%94.1 0%0.00000 <=Calc Antoine 0.0000 0.00 7.133 1516.79 174.95 0.00000
0 1.45 75.00 HCHO 0.20%30 0%0.00072 <=HCHO Eq.0.0007 0.00 na na na 0.00072
0 1.45 75.00 MeOH 0.00%32.04 0%0.00000 <=Calc Antoine 0.0000 0.00 7.897 1474.08 229.13 0.00000
0 1.45 75.00 Phenol 0.00%94.1 0%0.00000 <=Calc Antoine 0.0000 0.00 7.133 1516.79 174.95 0.00000
1,449 1.45 75.00 HCHO 0.10%30 0%0.00036 <=HCHO Eq.0.0004 0.00 na na na 0.00036
1,449 1.45 75.00 MeOH 0.00%32.04 0%0.00000 <=Calc Antoine 0.0000 0.00 7.897 1474.08 229.13 0.00000
1,449 1.45 75.00 Phenol 0.00%94.1 0%0.00000 <=Calc Antoine 0.0000 0.00 7.133 1516.79 174.95 0.00000
796,224 1.45 140.00 HCHO 50.50%30 100%0.30145 <=HCHO Eq.0.2723 0.00 na na na 0.30145
796,224 1.45 140.00 MeOH 1.50%32.04 100%0.18245 <=Calc Antoine 0.1760 0.00 7.897 1474.08 229.13 0.18245
0 1.45 90.00 HCHO 30.00%30 0%0.03981 <=HCHO Eq.0.0392 0.00 na na na 0.03981
0 1.45 90.00 MeOH 0.50%32.04 0%0.01746 <=Calc Antoine 0.0184 0.00 7.897 1474.08 229.13 0.01746
Methanol 0 1.45 59.28 NA MeOH 100.00%32.04 0%1.40988 <=Calc Antoine 1.5716 0.00 7.897 1474.08 229.13 1.40988
S = 0.6 for "Submerged" Tanker filling
S = 1.45 for "non Submerged" Tanker filling
S = 1.0 for Tote or Drum filling
365478
<==Not Controlled or vapor balanced
Resin Gallon with +5% OHAPs = 100,462 Enter 98% if Vapor Exchange is used or
Annual Throughput < 800,000 gal.No Controls Required (<800K Gal/yr)<==Transfer Racks loading liquids with +98% HAPs 100% if controlled by Oxidizer and accounted for in the HCHO plant emissions.
Annual Throughput (+10,000,000 gal) <10MM gal - No Controls Required<==Transfer Racks loading liquids with (5 - 97.9%) HAPs
Annual Throughput (+3,117,230 gal) Low Throughput Rack
<==Not Controlled or vapor balanced
Resin Gallon with +5% OHAPs = 235,431
Annual Throughput < 800,000 gal.No Controls Required (<800K Gal/yr)<==Transfer Racks loading liquids with +98% HAPs
Annual Throughput (+10,000,000 gal) <10MM gal - No Controls Required<==Transfer Racks loading liquids with (5 - 97.9%) HAPs
Annual Throughput (+3,117,230 gal) Low Throughput Rack
<==Not Controlled or vapor balanced
Resin Gallon with +5% OHAPs = 2,939,742
Annual Throughput < 800,000 gal.95% Controls or Vap. Bal Required<==Transfer Racks loading liquids with +98% HAPs
Annual Throughput (+10,000,000 gal) <10MM gal - No Controls Required<==Transfer Racks loading liquids with (5 - 97.9%) HAPs
Annual Throughput (+3,117,230 gal) Low Throughput Rack
<==Existing OLD Sources do not regulate drum/tote loading.
Resin Gallon with +5% OHAPs = 269,402
Annual Throughput < 800,000 gal.No Controls Required (<800K Gal/yr)<==Transfer Racks loading liquids with +98% HAPs
Annual Throughput (+10,000,000 gal) <10MM gal - No Controls Required<==Transfer Racks loading liquids with (5 - 97.9%) HAPs
Annual Throughput (+3,117,230 gal) Low Throughput Rack
Resin Gallon with +5% OHAPs = 3,275,636
Annual Throughput < 800,000 gal.Regulated Transfer Rack
Annual Throughput (+10,000,000 gal) <10MM gal - No Controls Required
Annual Throughput (+3,117,230 gal) High Throughput Rack
Resin Gallon with +5% OHAPs = 3,275,636
Annual Throughput <800,000 gal. Regulated Transfer Rack
Annual Throughput (+3,117,230 gal) High Throughput Rack
Table 7.1-5 Vapor Pressure Euqation Constants
HCHO 19.3 lb/yr Based on Celcius
MeOH 1,260.2 lb/yr A B C MW
Phenol 5.5 lb/yr HCHO Special Equation (based on K)30
EPI . lb/yr MeOH 7.897 1474.08 229.13 32.04
Ammonia . lb/yr Phenol 7.133 1516.79 174.95 94.1
MEK . lb/yr Formic 7.581 1699.2 260.7
N-Butanol .3 lb/yr EPI 8.2294 2086.806 273.16 92.05
Cresols . lb/yr Acetone 7.117 1210.595 229.664
MIBK . lb/yr
Check:OK
N
NA
NA
N
Y
N
N
N
Container
Y
Y
Y
Container
Y
Y
Container
Container
Container
N
Y
N
N
Y
Resimix (RPMX / RPMM)
OSB (RPPB)
Insulating Resins (RPPI)
Electrical Laminates (RPEL)
Hardboard (RPPD)
Abbrasives (RPAB)
Calculated "Other PF Resins (non-
specialty resins)"
Floral Foam (RPFM)
Filter Resins (RPLS)
High Pressure Laminates (RPHP)
RPPC 2112 Resin =
RPPC 2640 Resin =
RPPC 791C99 Resin =
OTHER (RPPC)
Saturating (RPPF)
Impregnating Resins (RPMS)
Loading Rack Emissions Summary
UFC
Resorcinol Resin - "RR" Total
UF / MUF Resin - "RU" Total
AF Resi Mix (COCM)
MF Resin - "RM" Total
AF Resin (CORM)
Formaldehyde
If Considered New Affected Source (OLD MACT)
If Considered Existing Affected Source (OLD MACT) - Speciality Load Rack
If Considered Existing Affected Source (OLD MACT) - Rail Loading
If Considered Existing Affected Source (OLD MACT) - PF Loading Rack
If Considered Existing Affected Source (OLD MACT) - Cumulative
If Considered Existing Affected Source (OLD MACT) - Container Loading
Georgia-Pacific Resins 5 CON_2021RY_EI_SARA 313_Calcs_FINAL
Resin Drying Pad_Air
Reporting Year 2021RY
Location Conway, NC
Fugitive Emissions Associated with Resin Solids Drying Pad
Background information
Plant Date of Test Liquid Resin Feed (type) MeOH (lbs / lbs wet feed)
HCHO (lbs /
lbs wet feed)
Phenol
(lbs / lbs
wet feed)
NH3 (lbs /
lbs wet
feed)
Chemical Volitalizati
on Rate
TAY Jan-09 351C05 0.002108203 0.00030603 4.37E-05 MeOH 30%estimated
CON Aug-06 217G77 0.003054484 0.00064934 0 HCHO 25%estimated
CON Aug-06 22C92 0.001767632 0.00021595 7.97E-05 0.000312 Phenol 10%estimated
0.002310106 0.00039044 4.11E-05 0.000312 Ammonia 100%worst case
Estimated %1,484,600
100%1,484,600 <-- estmated % based on production [UF & PF]/[total Resin]
100%1,484,600 <-- estmated % based on production [UF & PF]/[total Resin]
100% 1,484,600 <-- estmated % based on production [PF]/[total Resin]
50% 742,300 <-- estmated % based on production [UF & PF]/[total Resin]
Chemical of Concern Emission Factor Volitalization Rate Adjustment for % Liquid (4)
Drying Pad
Air Emissions
By Chemical
(lb/lb-liquid resin) (%) [10%/63%] (lb/yr)
Methanol 0.002310106 30%16%163
Formaldehyde 0.000390439 25%16%23
Phenol 4.11238E-05 10%16%1
Ammonia 0.000312032 100%16%37
(6) All data supporting these values are backed up in the Division's Spray Dryer Emissions Spreadsheet, tab "Division Summary_Emission Factors". The lbs/lbs emission factors are hidden
Emissions Factors developed from Divisional Test Data Provided by Decatur
Assumptions (this method is a best judgement estimate)
(1) A conservative estimate of air emission losses from the plant resin drying pad can be developed based on simple index of lbs of pollutant per pound of material placed on pad.
(2) Use Spray Dry Resins test data to represent the average consituents in the liquid resin. Data used is documented below.
(3) An average of the Taylorsville (2009) and Conway (2006) compound specific spray dry test results will be utilized to develop a generic index to be used by any facility that has a resin
(4) Resin solids on the pad are generated from fully or partially reacted resin. The emission factors are based on liquid based resin (typically ~37% solids & 63% liquid).
(5) Per R&D suggestion, resin drying pad volatilization rates: Methanol (0.30); Formaldehyde (0.25) ; Phenol (0.1)
AVERAGE =
Resin and Resin Solids to Drying Pad
Resins & Resin Solids to Drying Pad (lbs) =
Annual Resin Drying Pad Air Emissions
Percentage of Solids belived to contain MeOH
Percentage of Solids belived to contain HCHO
Percentage of Solids belived to contain Phenol
Percentage of Solids belived to contain Ammonia
Georgia-Pacific Chemicals LLC CON_2021RY_EI_SARA 313_Calcs_FINAL
Phenol Railcar Unloading
Reporting Year
Location
Phenol Railcar Emission Estimates:
Temperature Vapor Pressure Emission Rate Time Emissions
(oF)(PSI) (lbs/hr) (Hours) (lbs)
100 0.0195 0.091 1 0.091
110 0.0296 0.138 1 0.138
120 0.0440 0.205 1 0.205
130 0.0642 0.298 1 0.298
140 0.0920 0.428 1 0.428
150 0.1296 0.602 1 0.602
Total 6 1.762
Phenol Emissions Per Railcar (lbs):1.762 lbs.
Phenol Usage (lbs):78,473,113 lbs.
Number of Railcars Unloaded Annually:420
Annual Phenol Emissions From Railcars (lbs):740 lbs.
Notes:
Emissions Estimated by EPA TANKS4.0 Software Program.
Railcar dimensions are 48 feet by 9.5 feet.
Railcar holds 185,000 (lbs) or 20,740 (gal) of phenol.
Phenol is solid at 100F
Railcars are equiped with steam jackets
2021RY
Conway, NC
Georgia-Pacific Resins CON_2021RY_EI_SARA 313_Calcs_FINAL
OS-12
RESIN MANUFACTURING
LDAR Chemical Emissions (lbs/yr)
Methanol 2,366.83
Formaldehyde 491.76
Phenol 874.75
Cresols (Mixed)108.11
MEK 194.59
Loading Racks
Loading Rack Emissions Summary Emissions (lbs/yr)
HCHO 19.34
MeOH 1,260.17
Phenol 5.47
EPI -
Ammonia -
MEK -
N-Butanol 0.27
Cresols -
MIBK -
Drying Pad
Chemical of Concern Emission Factor Drying Pad Air Emissions By Chemical
(lb/lb-liquid resin)(lb/yr)
Methanol 0.002310106 163.31
Formaldehyde 0.000390439 23.00
Phenol 4.11238E-05 0.97
Ammonia 0.000312032 36.77
Cresol (lb/yr)108.1
Formaldehyde (lb/yr)534.1
Methanol (lb/yr)3,790.3
Phenol (lb/yr)881.2
Ammonia (lb/yr)36.77
MEK (lb/yr)194.59
VOC (tpy)2.75
OS-15
Thruput 11,587,854 gallons
VOC Emissions 0.00 ton/yr
Methanol Emissions 0.00E+00 lbs/yr
OS-10
Throughput (Each)1
HCHO 150
Methanol 716
Thruput 19,851 gallons
MEK Emissions 0.74 lb/yr
VOC Emissions 0.00 ton/yr
MEK/VOC Emission Factor 3.74E-05 lb/gallon
Thruput 703,953 gallons
Ammonia Emissions 278.66 lbs/yr
Emission Factor 1.5834E-03 lbs/gallon
Thruput 13,150,360 gallons
Pollutant Emissions (lbs/yr)Emission Factor (lb/gal)
Methanol 2,558.39 1.95E-04
Formaldehyde 3,037.83 2.31E-04
Acetaldehyde 20.13 1.53E-06
Emissions (tons/yr)
CO 4.57 3.47E-07
VOC 10.44 7.94E-07
Thruput 34,649,858 pounds
Annual Spray Dry Production (tons / yr)Calculated AVG Emission Factor (lb/ton)Emissions (lbs/yr) Emissions (tons/yr)Emission Factor (lb/lb)
MeOH 17,325 5.70 98,830 2.852E-03
HCHO 17,325 0.49 8,488 2.450E-04
Phenol (BDL)17,325 0.03 542 1.564E-05
Acetaldehyde (BDL)17,325 0.01 226 6.517E-06
Triethyamine (BDL)17,325 0.03 542 1.564E-05
Styrene (BDL)17,325 0.03 497 1.434E-05
Cresols (BDL)17,325 0.05 858 2.476E-05
Dimethyl Ether (DME)17,325 0.23 3,967 1.145E-04
Nox 17,325 0.54 9,294 4.65 2.682E-04
Ammonia 17,325 0.02 320 9.233E-06
CO 17,325 1.32 22,813 11.41 6.584E-04
VOC 56.98 tons/yr 3.289E-03
OS-40 Aqua Ammonia Tank
OS-1 Formaldehyde Plant
OS-54 Spray Dry Manufacturing
Spray Dryer Stack Test dated:
OS-44 MEK Tank
May 2019
Fugitive Sources-LDAR, Loading Racks, Drying Pad
Annual Resin Drying Pad Air Emissions
Summary
Methanol Storage Tank (Operating Under Primary Scenario)
Fugitive Sources - LDAR, etc from Formaldehyde plant (lbs/yr)
8 Kettles and 7 Weigh Tanks
Thruput 324,298,106 lbs
Pollutant Emissions lb/lb emission factor
Methanol 228.49 7.05E-07
Formaldehyde 22.29 6.87E-08
Phenol 1.02 3.14E-09
CO (tons)4.18 2.58E-05
Nox (tons)0.92 5.64E-06
EPI - 0.00E+00
HCL - 0.00E+00
VOC (tons)0.13 7.76E-07
Thruput 14,169,818 gallons
Emissions 0.00E+00 pounds
Throughput (gal/yr)1,542,292 Emission Factor (lb/gal)
HCHO (lbs)36.84 2.39E-05
MEOH (lbs)32.66 2.12E-05
VOC (tons)0.035 4.51E-05
Throughput (gal/yr)40,818,321 Emission Factor (lb/gal)
HCHO (lbs)15.01 3.68E-07
MEOH (lbs)837.21 2.05E-05
Phenol (lbs)3.76 9.22E-08
VOC (tons)0.43 2.097E-05
NOTE: According to AERO, OS-41 is for Tanks P11-P12. Should the description be updated to tanks S14-S17 & S21? P11-P12 are resin storage tanks.
Thoughput (gal/yr)2,381,178 Emission Factor (lb/gal)A little more to it. Let's discuss
HCHO(lbs)1.50 6.31E-07
MEOH (lbs)10.31 4.33E-06
Phenol (lbs)0.60 2.52E-07
VOC (tons)0.01 5.214E-06
Thruput 8,312,830 gallons Emission Factor (lb/gal)
Phenol (lbs)1,002.57 1.21E-04
VOC (tons)0.50 1.21E-04
Thruput 78,473,113 lbs Emission Factor (lb/lb)
Phenol (lbs)740.04 9.43E-06
VOC (tons)0.37 9.43E-06
Throughput (scf*1000/year)120,046 mscf/yr
CO2 7,161.89 tons/yr
Methane 0.13 tons/yr
N2O 0.01 tons/yr
TSP 22.81 tons/yr
PM10 22.81 tons/yr
PM2.5 22.81 tons/yr
SO2 0.04 tons/yr
Benzene 0.25 lbs/yr
Hexane, n-216.08 lbs/yr
Toluene 0.41 lbs/yr
Throughput (Gallons)215
CO2 2.42 tons/yr
CO 0.01 tons/yr
NOx 0.05 tons/yr
TSP 9.19E-04 tons/yr
PM10 8.50E-04 tons/yr
PM2.5 8.50E-04 tons/yr
SO2 0.00 tons/yr
VOC 1.36E-03 tons/yr
Acetaldehyde 7.47E-04 lbs/yr
Acrolein 2.34E-04 lbs/yr
Benzene 2.30E-02 lbs/yr
Formaldehyde 2.34E-03 lbs/yr
Napthalene (Component of
POMTV)3.85E-03 lbs/yr
Polycyclic Organic Matter (Inc.
PAH, Dioxins, etc)6.29E-03 lbs/yr
Toluene 8.33E-03 lbs/yr
Xylene 5.72E-03 lbs/yr
Throughput (scf*1000/year)18,051
CO2 1,076.93 tons/yr
Methane 0.02 tons/yr
N2O 2.03E-03 tons/yr
CO 0.76 tons/yr
NOx 0.90 tons/yr
TSP 0.07 tons/yr
PM10 0.07 tons/yr
PM2.5 0.07 tons/yr
SO2 0.01 tons/yr
VOC 0.05 tons/yr
Benzene 3.79E-02 lbs/yr
Formaldehyde 1.35E+00 lbs/yr
Hexane, n-32.49 lbs/yr
Toluene 6.14E-02 lbs/yr
Throughput (scf*1000/year)3,243
CO2 193 tons/yr
Methane 0.00 tons/yr
N2O 0.00 tons/yr
CO 0.14 tons/yr
NOx 0.16 tons/yr
TSP 0.01 tons/yr
PM10 0.01 tons/yr
PM2.5 0.01 tons/yr
SO2 0.00 tons/yr
VOC 0.01 tons/yr
Benzene 0.00681 lbs/yr
Formaldehyde 0.24322 lbs/yr
Hexane, n-5.83737 lbs/yr
Toluene 0.01103 lbs/yr
Throughput (lbs/yr)14,273,876
TSP 0.01 tpy
PM10 0.01 tpy
PM2.5 0.01 tpy
Throughput (lbs/yr)19,569,046
TSP 0.01 tpy
PM10 0.01 tpy
PM2.5 0.01 tpy
Throughput (scf*1000/year)7
CO2 0.40 tons/yr
Methane 7.51E-06 tons/yr
N2O 7.51E-07 tons/yr
CO 2.81E-04 tons/yr
NOx 3.34E-04 tons/yr
TSP 2.54E-05 tons/yr
PM10 2.54E-05 tons/yr
PM2.5 2.54E-05 tons/yr
SO2 2.00E-06 tons/yr
VOC 1.84E-05 tons/yr
Benzene 0.00001 lbs/yr
Formaldehyde 0.00050 lbs/yr
Hexane, n-0.01202 lbs/yr
Toluene 0.00002 lbs/yr
Throughput (scf*1000/year)25,995
CO2 3,030.70 tons/yr
Methane 0.03 tons/yr
N2O 0.00 tons/yr
NOx 1.30 tons/yr
TSP 0.10 tons/yr
PM10 0.10 tons/yr
PM2.5 0.10 tons/yr
SO2 0.01 tons/yr
Benzene 0.05 lbs/yr
Hexane, n-46.79 lbs/yr
Toluene 0.09 lbs/yr
Throughput (scf*1000/year)24,472
OS36-Urea Hopper for Reactor #8
OS33-Dowtherm Heater
OS20-Natural Gas Usage for CatOx
OS21-Natural Gas Usage for Thermal Oxidizer
OS-47 Phenol Unloading
OS55-NG Usage in Spray Dry Process
OS27-Industrial Engines (Generators)
OS3-NG/Propane Fired Boiler
OS37-Temporary Boiler
OS35-Urea Hopper for Reactor #3
OS-46 Phenol Storage Tanks
Total Emissions (lbs)
OS-13 Formaldehyde Raw Material Storage Tanks
OS-29 UF/UFC Resin Storage Tanks
OS-19 PF Resin Storage Tanks
OS41-Process Water Storage Tanks
OS-2 Resin Manufacturing
CO2 1,503.43 tons/yr
Methane 0.03 tons/yr
N2O 2.75E-03 tons/yr
TSP 0.09 tons/yr
PM10 0.09 tons/yr
PM2.5 0.09 tons/yr
SO2 0.01 tons/yr
Benzene 0.05 lbs/yr
Hexane, n-44.05 lbs/yr
Toluene 0.08 lbs/yr
1986
TSP 0.23 tons/yr
PM10 0.23 tons/yr
PM2.5 0.23 tons/yr
1986
TSP 0.23 tons/yr
PM10 0.23 tons/yr
PM2.5 0.23 tons/yr
1986
TSP 1.12 tons/yr
PM10 1.12 tons/yr
PM2.5 1.12 tons/yr
1980
TSP 0.15 tons/yr
PM10 0.14 tons/yr
PM2.5 0.12 tons/yr
VOC 10.10 tons/yr
1989
TSP 0.21 tons/yr
PM10 0.20 tons/yr
PM2.5 0.16 tons/yr
VOC 14.03 tons/yr
1980
TSP 8.26 tons/yr
PM10 1.65 tons/yr
PM2.5 0.41 tons/yr
NOx 7.98 tons/yr
PM10 (FIlterable)26.69 tons/yr
PM2.5 (FIlterable)25.38 tons/yr
SO2 0.06 tons/yr
TSP 33.22 tons/yr
VOC (as Carbon)82.63 tons/yr
Note: BDL = Below Detection Limit
sDATA - Total Summary Table
Paved Roads (PR-1)
OS51 - RM3 Extender Storage Silo (ES-11.1)
OS52 - RM4 Extender Storage Silo (ES-11.2)
OS50 - RESI-MIXER® (ES4.6)
OS-48 Cooling Tower (ES-T1A)
OS-49 Cooling Tower (ES-T3)
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-,,-,:.!M_sj��l.f9.m,J�d..t....eJl.ru.i
CataJv,jc Oxic:llur Stack Test da11d:
Con-
MeOH vusion
Plant PollvUin1 loom! Ratio
M•th.anol 23.0 1\.28
Formaldthyd• 23.0 11.28
RCI Act:taldt:hrde 23.0 11.28
Pla,it DME 23.0 11.28
VDC 23.0 11.28 co 23.0 11.28
Georgia•Paafic Resins
50%
HCHO
(tons/hr)
7 783
7 783
7.783
7.783
7.783
7.783
1,9.tZ < .. Ceilculeied Prod�n Ho1,111, beMd o,i 23gpm metl\enol f&edr,I&
-<••2021RV Actual run bme
. ··-·-·---OT Hours J f�"""!J 412612016
Oxidiz:■r Oxidizer
lnSet Ot.1tJet DRE """''' 110/hrl 1%1
19.97 D.32D 96.-611!.
18.70 0.380 OS.0"°
2.87 0.0025 99.9%
t0U7 2230 98.0%
131.4-4 281 98.0%
415.46 11'0 99.7%
UncontroUed
EmtSs.Rate f!OS11on1
2.57
2.40
0.37
14.12
1U9
53.38
t!Ot!Ol'l,illll1j
2•.2 •011 168.00 Res.Jn Plant
228 St)fl)'D�r
24,834 It
Annual etnt1.s1ons lrom Byoasses In Ubs):
Annual E11,;n1, � M•OH HCHO Acetafd• DME voe co Emlnlons ORE hyde
IHOUr$I
0 52 90% .0 1.0 0.1 5.7 8-8 21.8 a 00 75% 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 ao 0,0 a.o 0.0 0.0
o.o 0.0 a.o o.a o.o o.o
0.0 0.0 0.0 0.0 0.0 0.0
Total 1 1 a • 7 22
NOTE: Th& Conway RCI ptocess ts Interlocked lo ptevflnt bypa&s of HCHO Plant
·---
-c.'ti ...
St1011 flameout with minor Jow dett. T
Longer ftameouts ""1th low dettl T
Othor
OtMr
Othu
Other
CON_�1RY E!I SARA 313_Calcs_flNN..
Reportin g Year
Location � :Ji
..,, -wl'.:.i-t, lli
Fugitive Emissions Associated with Resin Solids Drying Pad
Assumption s (this method is a best judgement estimate)
Resin Drying Pad_Air
(I) A conservative estimate of air emission losses from the plant resin drying pad can be developed based on simple index of lbs of pollutant per pound of material placed on pad.
(2) Use Spray Dry Resins test data to represent the average consituents in the liquid resin. Data used is documented below
(3)An average of the Taylorsville (2009) and Com,a} (2006) compound specific spray dry test results will be utilized to develop a generic index to be used by any facility that has a resin
(4) Resin solids on the pad are generated from fully or partially reacted resin. The emission factors are based on liquid based resin (typically -37% solids & 63% liquid).
(5) Per R&D suggestion, resin drying pad volatilization rates: Methanol (0.30); Formaldehyde (0.25) ; Phenol (0.1)
l6) All data supporting these values are backed up in the Division's Spray Dryer Emissions Spreadsheet, tab "Division Summary Emission Factors".. The lbs/lbs emission factors are hidden
Backgroun d information
Emissions Factors devel oped from Divisional Test Data
Plant Date of Test Liquid Resin Feed {type) MeOH (lbs / lbs wet feed)
TAY Jan,09 351C05 0 002108203
CON Auq-06 217G77 0.003054484
CON AuQ-06 22C92 0.001767632
AVERAGE= 0.002310106
Resin and Resin Solids to Drying Pad
Resins & Resin Solids to Drying Pad (lbs)= I Estimated %
HCHO (lbs I
lbs wet feed)
0.00030603
0.00064934
0.00021595
0.00039044
Provided bt' Decatur
Phenol NH3 (lbs/
(lbs/ lbs lbs wet
wet feed) feed)
Chemical Volitalizati
on Rate
4.37E-05 ��i. MeOH 30%
0 ''"it;'i:.-"'Jll� HCHO 25%
7.97E-05 0.000312 Phenol 10%
4.11 E-05 0.000312 Ammonia 100%
estfmated
estimated
estimated
worst case
Percenta2e of Solids belived to contain MeOH 100%. 1 484 600 <-estmated % based on production [UF & PF]/[total Resin]
Percenta2e of Solids belived to contain HCHO 100% 1,484,600 <-estmated % based on production [UF & PF]/[total Resin]
Percentage of Solids belived to contain Phenol 100% 1,484,600 <-estmated % based on production [PF]/(total Resin)
Percenta2e of Solids belived to contain Ammonia 50% 742,300 <--estmated % based on production [UF & PF)/{total Resin]
n . �
Drying Pad
Chemical of Concern I Emission Factor I Volitalization Rate Adjustment for % Liquid ( 4) Air Emissions
By Chemical
lb/lb-Ii uid resin) % 10%/63%1 I (lb/yr'
Methanol 0.002310106 30% 16%
Formaldehyde 0.000390439 25% 16%
Phenol 4. I I 238E-05 10% 16%
Ammonia 0. 0003 I 2032 100% 16%
Georgia-Pacific Chemicals LLC CON_2021RY_EI_SARA 313_Calcs_FINAL
Phenol Railcar Unloading
Phenol Railcar Emission Estimates:
Temperature Vapor Pressure Emission Rate
(OF) (PSI) (lbs/hr)
0.0195 0.091
110 0.0296 0.138
120 0.0440 0.205
130 0.0642 0.298
140 0.0920 0.428
150 0.1296 0.602
Total
Phenol Emissions Per Railcar (lbs):
Phenol Usage (lbs):
Number of Railcars Unloaded Annually:
Annual Phenol Emissions From Railcars (lbs):
Notes:
Emissions Estimated by EPA TANKS4.0 Software Program.
Railcar dimensions are 48/eel by 9.5 feet.
Railcar holds 185,000 (lbs) or 20,740 (gal) of phenol.
Phenol is solid at I00F
Railcars are equiped with steam jackets
Time Emissions
(Hours) (lbs)
1 0.091
1 0.138
1 0.205
1 0.298
1 0.428
1 0.602
1.762
.___1._76_2 _ __.l lbs.
lbs.
lbs.
Georgia-Pacific Resins CON_2021 RY _EI_SARA 313_Calcs_FINAL
Thrupul
voe Emissions
Methanol Emissions
Thrupul
MEK Emissions
voe Emissions
MEKNOC Emisston Fae.tor
Thrupul
Arnmonla Emsslons
Emission Factor
Pollutant
Metnanot
Fonnaldef\yde
Ace\a1dehyde
MeOH
HCHO
Phenol(BOL)
Aeetaldehyde (BDL)
Tnelhya,mine-(BDL)
Stytene (BDL)
CtHWl(BOl)
Dim<e:thyi Ethet(OME)
Nox
Ammonia
Fuvh�ve Sourcea-LOAR, Loading Rack•� Drying Pad
Loadin Rac:k Emissions Summ
MeOH
Phenol
EPI
Ammonia
MEK
N•Bll1ano1
Cresols
MIBK
l�Pad Air Emissions
Emission Faetot'
lbllb-U uld rttln
0.002310\06
0.000390439
4.11238E-05
0.000312032
Cr�Obly,)
F-aldehy<le Ob/yr)
Melhanol Ob/yr)
Phenol Ob/yr)
Ammonia Ob/yr)
MEK 0blyr)
VQC I
Emissions (lbs/
Summary
Methanol Storage Tank (Operating Under Primary Scenario�
1 \ ,587 ,8S4 gallons
000 Ion/yr
0.OOE+OO I
Chemical
163.31
23.00
097
36.77
108.1
S34_1
3.790.3
881.2
36.77
194.59
H�
Fughlve Sources• LOAR:, etc rrom ,:ormaldetayde plant (lbs/yr)
TJ,toughpul (Each) I
H�O 150
Methanol 716
17,325
17,325
17,325
17,325
17,325
17,325
17,325
17,325
17,325
17,325
17.325
19,851 gallons
0.74 lb/yr
0.00 Ion/yr
:l 7•E-05 11>1 allon
703,953 gallOflJ
27Ull lbs/'jr
1.5834E-03 lbs lion
Emissk>n Fattor (lb/gal)
\.95E-04
2.31E·04
\.53E 06
3.47E-07
7.94E-07
$698
Em1 .. 1ono (tonOlyrl Emluion •·actor (lb/lb)
2.852 -03
2.•50E-04
1.564E-05
6.517E-06
1.564E-05
1.434E-05
2.476E-05
I 145E-04
2 882E 04
9 233E-06 1141 6584E 04
---------------- ----------05·2 Resin Ma nufacturmg TM,put
Pollutant Methanol Formaldehyde­Phenol cd'jfonsr !'!211.� �Pl >fCL 110!:"llons
Total Emissions (lbs)
Emlssk>ns
1€56@ fl A®·ik54if W·Ufoiiti
rhrupul Emissions
Thrcughpu1 (gal/yr) HCHOpbs) MEOHpbs) VOC.flons
Thrcughpu1 (gal/yr) HCHOPbs) MEOHPbs) Phenol Pbs) VOC Ions
Thoughpu1 (gal/yr) HCHOpbs) MEOHpbs) Phenol pbs) voe ions
Thtuput PloMol Pbsl voe ons
Thrupul Phenol Qbs) voe ons
Throughpu1 (strtOOOlyear) CO2 Methane
N20 TSP PM10 PM2 5 S02
Benzel\6 11iu1;:ine, n Toluene
,._ 16'A11 0011!';+011
1 542,292 38.84 32.66 0.035
0S27 lndu�tnal E_ng,n�s (Generators} Throughpu1 (Gallons) CO2 co NOX TSP PM10 PM2 5 502
voe Acet;ldehyde Acro1e,n
Benzene Formaldehyde Nap1halene (Component of POMTV) Pol)'cy<lic organic Matter (Int. PAI-I. Dioxins, ett) TOiuene Xylene
0S3-NGIPropane Fired 801ler Throughpu1 (scr 1000,'Jeari CO2 Metl'liloe
N20 co NOx TSP PMtO PM2 5 S02 voe Benzene, Formaldehyde Hexane, n-Toluene
8 Kettles �nd 7 Weigh Tank, 324.298.106 lbs
2211.49 22.29 1.02 "lf C,
�l� __ _,..,... 7.05E-07
4�.iltB,321 15.01 837.21 3.76 00
2,381,178 1.50 10 .31 0.60 0.01
8,312,830 gallons 1,002 57 0.50
78,473.113 lbs 740.04 0.37
120,048 mscf/yr 7181 89 Ions/yr 01 3 lonsfyr 001 tons/yr 22 81 tonstyr 2281 tonsr,, 2281 tons/yr 004 tonstyr 025 lbstyr 218.0B lbsfyr 0.,1 lbs,Yr
215 2.,2 tons/yr 0.01 tons,yr 0.05 tons/yr 9.19E·04 tonsl)'r 8.SOE·04 tons/yr 8.SOE 04 tons/yr 0.00 tons/yr 1.36E 03 1ons1yr 7.47E 04 lbs/yr 2.34E 04 lbs/yf 2.30E 02 lbs/yr 2 34E 03 lbs/yr
3.85E 03 lbs/yr
6.29E,03 lbsl)'r B.33E-03 lbSl)'r 5.72E 03 lbs/yr
18,051 1,076.93 tons/yr 0.02 tons/yr 203E-03 tonslys 076 tons/yr 0.90 tons/yr 0.07 tonslyr 007 lons/)lr 007 1D0$/IJT 0.01 tonsl)'r 0.05 Ion.,.,_., 3.79E•02 lbs/yr t 35E+OO lbs/yr 32.49 lbsl'fr B 14E-02 lbsl)'r
6.87E-OB 3.1 4E-09 2� 5��06 O.OOE•OO O.OOE+OO nn•:01
t..ltlllll> ,.010< �jl) 2.39E-05 212E-05 4.51E•OS
Emission Fae.tar Ob/gaY;I 3.68E-07 2.0SE-05 9.22E-OB 2.097E•OS
EmiSSIOO F1ct a,(lblg ai;I 6.JIE-07 4-JJE-06 2.S2E-07 5.214E 06
Emission Factor (lb/gJJIJ l.21E•04 l.21E•04
Emission Factor (1�1 9.43E-06 9.43E-06
0S37-Temporary Boiler
co
voe
0S33-Dowttierm Healer
voe
7
2
o.
voe
NO•
voe as Cal'bo1t
Emission Equipment Description:
Emission Unit ID No.:
Maximum Ho urly Heat Input (MMBtu/hr):
Annual Natural Gas Usage (set/yr):
Annual Natural Gas Usage (MMBtu/yr):
HHV of Natural Gas (Btu/sd):
Criteria Emissions from the Boiler (ES-B1)
Compound
PM (Filterable)
PM10/ PM2.5 (Condensable)
PM10 (Total)
PM2_5 (Total}
NOx co
S02 voe
Lead (Pb)
Total GHGb
Total C0 2e b
Permanent Boiler -OS-3
ES-Bl
25.1
18,051,215
18,412
1,020
Em1ss1on
Factor"
fib/MM Btu)
l.86E-03
S.59E-03
7.45E-03
7.45E-03
9.BOE-02
8.24E-02
5.88E-04
S.39E-03
4.90E-07
116.98
117.10
219,876
Emission Rate c,d
(lb/hr) (tpv)
0.05 0.02
0.14 0.05
0.19 0.07
0.19 0.07
2.46 0.90
2.07 0.76
0.01 0.01
0.14 0.05
1.23E-05 4.SlE-06
2,936 1,077
2,939 1,078
a.AP-42 Section 1.4, Natural Gas Combustion (July 1998), Tables 1.4-1 and 1.4-2, converted from
lb/MMscf to lb/MMBtuusing the heating value of 1,020 Btu/scf.
PM 10 (Total) and PM 2 .s (Total) assumed the same and include both filterable plus condensable emissions.
b.EPA's Mandatory Reporting Rule for Greenhouse Gases, 40 CFR Part 98, Subpart C, Tables C-1 and C-2.
c.Emission Rate (lb/hr)= Emission Factor (lb/MMBtu) * Hourly Heat Input (MMBtu/hr)
d.Emission Rate (tpy) = Emission Factor (lb/MMBtu) * Annual Heat Input {MM Btu/yr) * (ton/2,000 lb)
HAP Emissions from the Bo iler (ES-B1)
Compound
Benzene
Formaldehyde
Hexane
Naphthalene
Polycyclic Organic Matter
Toluene
METAL HAP
Arsenic Compounds
Cadmium Compounds
Chromium Compounds
Cobalt Compounds
Lead Compounds
Manganese Compounds
Mercury Compounds
Nickel Compounds
Em1ss1on
Factor"
(lb/MM Btu)
2.06E-06
7.35E-05
l.76E-03
5.98E-07
6.49E-07
3.33E-06
1.96E-07
l.08E-06
l.37E-06
8.24E-08
4.90E-07
3.73E-07
2.SSE-07
2.06E-06
Total HAP
Emission Rate b,c
(lb/hr) (tpy)
5.17E-05 l.90E-05
1.85E-03 6.77E-04
4.43E-02 0.02
1.SOE-05 5.SlE-06
1.63E-05 5.97E-06
8.37E-05 3.07E-05
4.92E-06 1.81E-06
2.71E-05 9.93E-06
3.45E-05 1.26E-05
2.07E-06 7.58E-07
1.23E-05 4.SlE-06
9.35E-06 3.43E-06
6.40E-06 2.3SE-06
5.17E-05 1.90E-OS
0.05 0.02
a.AP-42 Section 1.4, Natural Gas Combustion (July 1998), Table 1.4-3 for organic HAP and Table 1.4-4
for metal HAP, converted from lb/MMscf to lb/MM Btu using the heating value of 1,020 Btu/scf.
b.Emission Rate (lb/hr)= Emission Factor (lb/MM Btu)* Hourly Heat Input {MM Btu/hr)
c.Emission Rate (tpy) = Emission Factor (lb/MM Btu) • Annual Heat Input (MM Btu/yr) * (ton/2,000 lb)
Emission Equipment Description:
Emission Unit ID No.:
Maximum Hourly Heat Input (MM Btu/hr):
Annual Natural Gas Usage (sd/yr):
Annual Natural Gas Usage (MMBtu/yr):
HHV of Natural Gas (Btu/scf):
Criteria Emissions from the Boiler (ES-B2)
Compound
PM (Filterable)
PM 1o/PM 2_5 (Condensable)
PM 10 (Tota l}
PM2_5 (Total)
NOx co
SO2 voe
Lead (Pb}
Total GHGb
Total CO2eb
Temporary Boiler -OS-37
ES-B2
25
3,242,982
3,308
1,020
Emission
Factor8
(lb/MM Btu)
1.86E-03
S.59E-03
7.4SE-03
7.4SE-03
9.B0E-02
8.24E-02
S.88E-04
S.39E-03
4.90E-07
116.98
117.10
Emission Rate c,d
(lb/hr) (tpy)
0.05 3.08E-03
0.14 9.24E-03
0.19 l.23E-02
0.19 1.23E-02
2.45 1.62E-01
2.06 l.36E-01
0.01 9.73E-04
0.13 8.92E-03
1.23E-0S 8.llE-07
2,924 193
2,927 194
a.AP-42 Section 1.4, Natural Gas Combustion (July 1998), Tables 1.4-1 and 1.4-2, converted from
lb/MMscf to lb/MMBtuusing the heating value of 1,020 Btu/set.
PM10 (Total) and PM2_5 (Total) assumed the same and include both filterable plus condensable emissions.
b.EPA's Mandatory Reporting Rule for Greenhouse Gases, 40 CFR Part 98, Subpart C, Tables C-1 and C-2.
c.Emission Rate (lb/hr)= Emission Factor (lb/MM Btu)* Hourly Heat Input (MMBtu/hr)
d.Emission Rate (tpy) = Emission Factor (lb/MM Btu) * Annual Heat Input (MMBtu/yr) * (ton/2,000 lb)
HAP Emissions from the Boil er (ES-B2)
t.m1ss1on Emission Rate b,, Compound Factor8
(lb/MMBtu) (lb/hr) (tp y) Benzene 2.0GE-06 S.lSE-05 3.41E-06
Formaldehyde 7.3SE-0S 1.84E-03 1.22E-04
Hexane 1.76E-03 4.41E-02 2.92E-03
Naphthalene S.98E-07 l.S0E-05 9.89E-07
Polycyclic Organic Matter 6.49E-07 1.62E-05 1.07E-06
Toluene 3.33E-06 8.33E-05 S.SlE-06
METAL HAP
Arsenic Compounds 1.96E-07 4.90E-06 3.24E-07
Cadmium Compounds 1.08E-06 2.70E·OS 1.78E-06
Chromium Compounds 1.37E-06 3.43E-05 2.27E-06
Cobalt Compounds 8.24E-08 2.0GE-06 1.36E-07
Lead Compounds 4.90E-07 1.23E-05 8.llE-07
Manganese Compounds 3.73E-07 9.31E-06 6.16E-07
Mercury Compounds 2.SSE-07 6.37E-06 4.22E-07
Nickel Compounds 2.0GE-06 S .lSE-05 3.41E-06
Total HAP 0.05 3.06E-03
a.AP-42 Section 1.4, Natural Gas Combustion (July 1998), Table 1.4-3 for organic HAP and Table 1.4-4
for metal HAP, converted from lb/MMscf to lb/MM Btu using the heating va1ue of 1,020 Btu/scf.
b.Emission Rate (lb/hr)= Emission Factor (lb/MM Btu) * Hourly Heat Input (MM Btu/hr)
c.Emission Rate (tpy) = Emission Factor (lb/MMBtu} * Annual Heat Input (MM Btu/yr) * (ton/2,000 lb)
Emission Equipment Description:
Emission Unit ID No.:
Diesel Engines -OS-27
ES-GENl
Maximum Hourly Heat Input (hp/hr): 755
Fuels Fired: Diesel
Annual Heat Input (hp/yr): 4,236
Criteria Emissions from the Diesel-Fired Generator (ES-GEN1)
Compound Emission Factor"
(lb/hp-hr)
PM (Filterable) 4.34E-04
PM10 (Total} 4.0lE-04
PM2.5 (Total) 4.0lE-04
NOx 2.40E-02 co 5.S0E-03
SO2 l.21E-05voe 6.42E-04
Total GHGb 1.14
Total CO2eb 1.15
' Emission Rate c,d
(lb/hr) (tpy)
0.33 9.19E-04
0.30 8.50E-04
0.30 8.50E-04
18.12 0.05
4.15 0.01
9.16E-03 2.57E-05
0.48 l.36 E-03
862 2.42
865 2.43
a.Compounds other than Particulate emissions from AP-42 Section 3.4, Large Stationary Diesel and All
Stationary Duel-fuel Engines (October 1996), Table 3.4-1.
Diesel fuel sulfur content(%} 0.0015
Particulate emissions per AP-42 Section 3.4, Large Stationary Diesel and All Stationary Duel-fuel
Engines (October 1996), Table 3.4-2, converted from lb/MM Btu to lb/hp-hr using an average brake­
specific fuel consumption (BSFC) of 7,000 Btu/hp-hr from AP-42, Section 3.3, Table 3.4-1.
PM 10 (Total) and PM 2_5 (Total) assumed the same and include both filterable plus condensable emissions.
b.GHGs from EPA's Mandatory Reporting Rule for Greenhouse Gases, 40 CFR Part 98, Subpart C, Tables
C-1 and C-2, converted from lb/MM Btu to lb/hp-hr using an average brake-specific fuel consumption
(BSFC) of 7,000 Btu/hp-hr from AP-42, Section 3.3, Table 3.3-1.
c.Emission Rate (lb/hr)= Emission Factor (lb/hp-hr) * Engine Rating (hp)
d.Emission Rate (tpy) = Emission Rate (lb/hr)* Hours of Operation {hr/yr)• {ton/2,000 lb}
HAP Emissions from the Diesel-Fired Generator (ES-GEN1)
Compound Emission Factora
{lb/hp-hr)
Acetaldehyde 1.76E-07
Acrolein 5.52E-08
Benzene 5.43E-06
Formaldehyde S.52E-07
Naphthalene 9.l0E-07
Polycyclic Organic Matter l.48E-06
Toluene l.97E-06
Xylenes (Mixed Isomers) 1.35E-06
Total HAP
Emission Rate b,c
(lb/hr) (tpy)
l.33E-04 3.74E-07
4.16E-05 l.17E-07
4.lOE-03 l.lSE-05
4.17E-04 l.17E-06
6.87E-04 1.93E-06
l.12E-03 3.14E-06
1.49E-03 4.17E-06
l.02E-03 2.86E-06
9.0lE-03 2.53£-05
a.AP-42 Section 3.4, Large Stationary Diesel and All Stationary Duel-fuel Engines (October 1996}, Table 3.4-3,
converted from lb/MM Btu to lb/hp-hr using an average brake-specific fuel consumption (BSFC)
of 7,000 Btu/hp-hr from AP-42, Section 3.4, Table 3.4-1.
Emission Equipment Description:
Emission Unit ID No.:
Control Device Description:
Maximum Methanol Feed Rate:
Average Conversion Ratio:
Maximum Hourly HCHO Production Rate:
Maximum Annual HCHO Production Rate:
Maximum Hourly Heat Input:
Annual Natural Gas Usage (sd/yr):
Annual Natural Gas Usage (MMBtu/yr):
HHV of Natural Gas:
Formaldehyde (HCHO) Manufacturing Process (VS2A) • Natural Gas Combustion Only
Formaldehyde Production Process (ES-2)
Formaldehyde Tank Truck Loading Rack (ES·FL)
One Methanol Storage Tank (ES3Ml)
Eight Formaldehyde/Methanol Storage Tanks (ES7Fl-F8)
Catalytic Oxidizer (CD-2A)
32 gallons per min (gpm)
11.28 lbs. 50% HCOH/gallon MEOH
10.83
74,168
4.0
25,995,073
26,515
1,020
tons/hr
tons/yr
MMBtu/hr
Btu/scf
Criteria Emissions h rom t e Formal d h d e ,y e Manu acturing Process Nb Em1ss1on Process
Compound Factor• Related b
(lb/MM Btu) (lb/ton)
PM (Filterable) l.86E-03 ..
PM 1o/PM 25 (Condensable) S.59E-03 ..
PM 10 (Total) 7.45E-03 ..
PM2 .5 (Total) 7.45E-03 ..
NOx 9.80E-02 ..
S0 2 5.88E-04
Lead (Pb) 4.90E-07
Total GHG0 116.98 39.91
Total co2e• 117.10 39.91
Emission Rate d,e
!lb/hr)(tnvl
0.01 0.02
0.02 0,07
0.03 0.10
0.03 0.10
0.39 1.30
2.35E-03 0.01
l.96E-06 6.SOE-06
900 3,031
901 3,032
a.AP-42 Section 1.4, Natural Gas Combustion (July 1998), Tables 1.4·1 and 1.4-2, converted from
lb/M Mscf to lb/M MB tu using the heating value of 1,020 Btu/scf.
PM 10 (Total) and PM 2•5 (Total) assumed the same and include both filterable plus condensable emissions.
b. Emission factors based on Stack Test dated 4/26/2016.
c. EPA's Mandatory Reporting Rule for Greenhouse Gases, 40 CFR Part 98, Subpart C, Tables C·l and C-2.
d.Emission Rate (lb/hr)= Emission Factor (lb/MM Btu)• Hourly Heat Input (MMBtu/hr)
Emission Rate (lb/hr) = Emission Factor (lb/ton) • Hourly HCHO Production Rate (ton/hr) • (1 • DRE(%))
e.Emission Rate (tpy) = Emission Factor (lb/MMBtu) • Annual Heat Input (MMBtu/yr) • (ton/2,000 lb)
Emission Rate (tpy) = Emission Factor (lb/ton) • Annual HCHO Production Rate (tons/yr) • (ton/2,000 lb) • (1-DRE(%))
HAP Emissions from t e Formalde 1y, e Manu acturing Process h h d Nb Em1ss1on Process Emission Rate b.c Compound Factor" Relatedb
(lb/MMBtul (lb/ton) llb/hrl (tpvl Benzene 2.0GE-06 ..8.24E-06 2.73E-OS
Hexane 1.76E-03 7.0GE-03 0.02
Naphthalene 5.98E•07 --2.39E-06 7.93E-06
Polvcvclic Organic Matter 6.49E-07 ..2.GOE-06 8.GOE-06
Toluene 3.33E-06 .. 1.33E·OS 4.42E·OS
METAL HAP
Arsenic Compounds 1.96E-07 .. 7.84E-07 2.GOE-06
Cadmium Compounds 1.08E-06 ..4.31E-06 1.43E-OS
Chromium Compounds 1.37E-06 --5.49E-06 1.82E-OS
Cobalt Comoounds 8.24E-08 -·3.29E-07 1.09E-06
Lead Comoounds 4.90E-07 --1.96E·06 6.SOE-06
Man2anese Comoounds 3.73E-07 .. 1.49E-06 4.94E-06
Mercurv Compounds 2.SSE-07 --1.02E-06 3.38E-06
Nickel Compounds 2.0GE-06 -·8.24E-06 2.73E-OS
Total HAP 0.01 0.02
a.AP-42 Section 1.4, Natural Gas Combustion (July 1998), Table 1.4-3 for organic HAP and Table 1.4·4
for metal HAP, converted from lb/MMscf to lb/MMBtu using the heating value of 1,020 Btu/scf.
b.Emission Rate (lb/hr)= Emission Factor (lb/MMBtu) • Hourly Heat Input (MMBtu/hr)
c. Emission Rate (tpy)" Emission Factor (lb/MMBtu) • Annual Heat Input (MM Btu/yr)• (ton/2,000 lb)
Emission Equipment Description:
Emission Unit ID No.:
Control Device Description:
Maximum Hourly (UF + PF) Resin Production Rate:
Maximum Annual Resin Production Rate:
Maximum Hourly Heat Input:
Annual Natural Gas Usage (scf/yr):
Annual Natural Gas Usage (MM Btu/yr):
HHV of Natural Gas:
Resin Manufacturing Process (VS4A.l & VS4A.2] -Emissions From Natural Gas Combustion Only
TP-n Resin Vessels including
Four batch non-reactor vessels which includes-
Three Weigh Tanks (ES4.9 -4.11 and one Mix/Blend Tank (S-13)
and six Batch Reactor Vessels ( ES4.1 through 4.3, ES4.5, ES4. 7, & ES4.81
Alternate Compliance Scenario
One Methanol Storage Tank (ES3Mll
Eight Formaldehyde/Methanol Storage Tanks {ES7Fl-F8 )
Thermal Oxidizer (CD-4A)
38 tons/hr
162,149 tons/yr
2.9 MM Btu/hr
24,471,733
24,961
1,020 Btu/scf
CI I E •• r ter a m1ss1ons rom e esin anu actur nl! th R . M p rocess ""' tm1ss1on Process Emission Rate d,• Compound Factor• Related•
(lb/MMBtu) (lb/ton Resinl (lb/hr)
PM (Filterable\ 1.86E-03 --0.01
PM1o/PM 2_5 (Condensable) S.59E-03 .. 0.02
PM10 (Total) 7.45E-03 --0.02
PM2.s (Total) 7.45E-03 --0.02
S02 S.SSE-04 1.71E-03
Lead (Pb) 4.90E-07 1.42E-06
Total GHG' 116.98 S.36E-01 359
Total C02e' 117.10 S.36E-Ol 360
a.AP-42 Section 1.4, Natural Gos Combustion (July 1998), Tables 1.4-1 and 1.4-2, converted from
lb/MMscf to lb/MM Btu using the heating value of 1,020 Btu/scf.
(tovl
0-02
0.07
0.09
0.09
0.01
6.12E-06
1,503
1,505
PM 10 (Total I and PM 2•5 (Total) assumed the same and include both filterable plus condensable emissions.
b.Emission factors based on Stack Test dated 4/26/2016.
c.EPA's Mandatory Reporting Rule for Greenhouse Gases, 40 CFR Part 98, Subpart C, Tables C-1 and C-2.
d.Emission Rate (lb/hr)= Emission Factor (lb/MMBtu) • Hourly Heat Input {MM Btu/hr)
Emission Rate (lb/hr)= Emission Factor (lb/ton)• Hourly (UF + PF) Resin Product,on Rate {ton/hr) • (1 -ORE(%))
e.Emission Rate (tpy) = Emission Factor (lb/MMBtu) • Annual Heat Input (MMBtu/yr) • {ton/2,000 lb)
Emission Rate (tpy) = Emission Factor (lb/ton)• Annual (UF + PF) Resin Production Rate (tons/yr)• (ton/2,000 lb)• (1 -DRE(%))
HAP Em1ss1ons f h romt e Resin Manu acturing Process rtu cm1ss1on
Compound Factor•
Process
Related Emission Rate b,c
llb/MMBtu) (lb/ton) (lb/hr)
Benzene 2.06E-06 --S.97E 06
Hexane 1.76E-03 S.l2E-03
Naphthalene 5.98E-07 --1.73E-06
Po[vrvclic On1anic Matter 6.49E-07 --1.88E-06
Toluene 3.33E-06 --9.67E-06
METAL HAP
Arsenic Compounds 1.96E-07 ..S.69E-07
Cadmium Compounds 1.0SE-06 ..3.13E-06
Chromium Compounds 1.37E-06 --3.98E-06
Cobalt Comoounds 8.24E-08 --2.39E-07
Lead Comoounds 4.90E-07 --1.42E-06
Manl!anese Comoounds 3.73E-07 --1.0SE 06
Mercurv Compounds 2.SSE-07 -7.39E-07
Nickel Compounds 2.0GE-06 -5.97E-06
Total HAP 0.01
a.AP-42 Section 1.4, Natural Gas Combustion (July 1998), Table 1.4-3 for organic HAP and Table 1.4-4
for metal HAP, converted from lb/MMscf to lb/MMBtu using the heating value of 1,020 Btu/scf.
b.Emission Rate (lb/hr) = Emission Factor (lb/MMBtu) • Hourly Heat Input (MMBtu/hrl
c. Emission Rate (tpy) = Emission Factor (lb/MMBtu) • Annual Heat Input (MMBtu/yr) • (ton/2,000 lb)
(tpy) 2.57E-05
0.02
7.46E·06
8.lOE-06
4.16E-05
2.45E-06
1.35E-05
1.71E-OS
1.03E-06
6.12E-06
4.6SE·06
3.lSE-06
2.57E-05 o.oz
Emission Equipment Description:
Emission Unit ID No.:
Control Device Description:
Maximum Hourly Heat Input:
Annual Natural Gas Usage (scf/yrl:
Annual Natural Gas Usage (MMBtu/yr):
Fuels Fired:
HHV of Natural Gas:
Bagfilter (CD·SA) flowrate
Annual Hours of Operation:
Spray Dry Resin Manufacturing Process (VSSA) • Emissions From Natural Gas Combustion Only
Spray Dry Resin Process (ES·S) Including
Natural Gas Fired Atomizing Air Heater
Spray Dryer
Several Transfer Cyclones and a Product Bagging Operation
Bagfilter (CO-SA)
14.6 MM Btu/hr
120,045.956
122,447
Natural Gas
1,020
65,000
8,188
Btu/scf
dscfm
hr/yr
Criteria Emissions from the Sorav Orv Resin Manufacturing Process Nb Em1ss1on Process Emission Rate d.• Compound Factor• Related b
llb/MMBtul lib/ton) llb/hr)
PM/PM 1o/PM2.s .. 0.01 gr/dscf 5.57
S02 5.88E-04 8.59E 03
Lead (Pb) 4.90E-07 7.16E -06
Total GHG" 116.98 ..1,708
Total C02e" 117.10 .. 1,710
a.AP-42 Section 1.4, Natural Gas Combustion (July 1998), Tables 1.4-1 and 1.4-2, converted from
lb/MMscf to lb/MM Btu using the heating value of 1,020 Btu/scf.
(tpy)
22.81
0.04
3.00E-05
7,162
7,169
CO and NOx emissions from the natural gas combustion were included with process emissions calculations.
b.PM/PM 1of PM zs emission factors based on engineering estimate.
c.EPA's Mandatory Reporting Rule for Greenhouse Gases, 40 CFR Part 98, Subpart C, Tables C-1 and C-2.
d.Emission Rate (lb/hr)= Emission Factor (gr/dscf) • Maximum Air Flow Rate (dscfm) • (lb/7,000 grl • (60 min/hr)
Emission Rate (lb/hr)= Emission Factor (lb/MM Btu)• Hourly Heat Input (MMBtu/hr)
Emission Rate (lb/hr) = Emission Factor (lb/ton) • Hourly Dry Resin Production Rate (ton/hr)
e.Emission Rate (tpy) = Emission Factor (gr/dscf) • Maximum Air Flow Rate (dscfm) • (lb/7,000 gr)• (ton/2,000 lb)• (60 min/hr)• (8,760 hr/yr}
Emission Rate (tpy) = Emission Factor (lb/MM Btu)• Annual Heat Input (MM Btu/yr)• (ton/2,000 lb)
HAP Emissions h rom t e Spray Dry Resin Manu acturing p rocess NU Em1ss1on
Compound Factor•
llb/MMBtul
Benzene 2.06E·06
Hexane l.76E-03
Naphthalene 5.98E-07
Polvcvclic OrRanic Matter 6.49E-07
Toluene 3.33E-06
METAL HAP
Arsenic Compounds l.96E-07
Cadmium Compounds l.OSE-06
Chromium Compounds ·1.37E-06
Cobalt Compounds 8.24E-08
Lead Comoounds 4.90E-07
ManRanese Compounds 3.73E-07
Mercury Compounds 2.SSE-07
Nickel Compounds 2.06E-06
Process
Related
llb/tonl .. .. .. .. ..
.. ·-
..
.. --
.. ·-
..
Total HAP
Emission Rate b,c
!lb/hr)(tpvl
3.0lE-05 1.26E-04
2.58E-02 l.OSE-01
8.73E-06 3.66E-05
9.47E-06 3.97E-05
4.87E-OS 2.04E-04
2.86E-06 1.20E-05
1.57E-OS 6.60E-05
2.00E-05 8.40E-05
1.20E-06 5.04E-06
7.16E-06 3.00E-05
S.44E-06 2.28E-05
3.72E-06 l.56E-05
3.0lE-05 1.26E-04
0.03 0.11
a.AP-42 Section 1.4, Natural Gas Combustion (July 1998), Table 1.4-3 for organic HAP and Table 1.4-4
for metal HAP, converted from lb/MMscf to lb/MM Btu using the heating value of 1,020 Btu/scf.
b.Emission Rate (lb/hr)= Emission Factor (lb/MM Btu)• Hourly Heat Input (MMBtu/hr)
c.Emission Rate (tpy) = Emission Factor (lb/MM Btu) • Annual Heat Input (MM Btu/yr)• (ton/2,000 lb)
Emission Equipment Description:
Emission Unit ID No.:
Maximum Hourly Heat Input (MM Btu/hr):
Annual Natural Gas Usage (scf/yr):
Annual Natural Gas Usage (MMBtu/yr):
HHV of Natural Gas (Btu/scf):
Natural Gas fired Heat Transfer Fluid Heater
ES-HTF
2.3
6,680
6.81
1,020
Criteria Emissions from the Heat Transfer Fluid Heater (1-HTF) Em1ss1on
Compound Factora
(lb/MM Btu)
PM (Filterable) l.86E-03
PM 10 / PM 2.5 (Condensable) 5.59E-03
PM10 (Total) 7.45E-03
PM2 •5 (Total) 7.4SE-03
NOx 9.80E-02 co 8.24E-02
SO2 5.88E-04
voe S.39E-03
Lead (Pb) 4.90E-07
Total GHG b 116.98
Total CO2eb 117.10
Emission Rate c,d
(lb/hr) (tpy)
4.28E-03 6.35E-06
1.29E-02 1.90E-05
1.71E-02 2.54E-05
1.71E-02 2.54E-05
2.25E-01 3.34E-04
1.89E-01 2.81E-04
l.35E-03 2.00E-06
1.24E-02 1.84E-0S
l.13E-06 1.67E-09
269 0.40
269 0.40
a.AP-42 Section 1.4, Natural Gas Combustion (July 1998), Tables 1.4-1 and 1.4-2, converted from
lb/MMscf to lb/MMBtuusing the heating value of 1,020 Btu/set.
PM 10 (Total) and PM2.5 (Total} assumed the same and include both filterable plus condensable emissions.
b.EPA's Mandatory Reporting Rule for Greenhouse Gases, 40 CFR Part 98, Subpart C, Tables C-1 and C-2.
c.Emission Rate (lb/hr)= Emission Factor (lb/MMBtu) * Hourly Heat Input {MM Btu/hr)
d.Emission Rate {tpy) a: Emission Factor {lb/MMBtu) * Annual Heat Input (MM Btu/yr) * (ton/2,000 lb)
Potential HAP Emissions from the Heat Transfer Fluid Heater (1-HTF)
Compound
Benzene
Formaldehyde
Hexane
Naphthalene
Polycyclic Organic Matter
Toluene
METAL HAP
Arsenic Compounds
Cadmium Compounds
Chromium Compounds
Cobalt Compounds
Lead Compounds
Manganese Compounds
Mercury Compounds
Nickel Compounds
Em1ss1on
Factora
(lb/MMBtu)
2.06E-06
7.3SE-0S
1.76E-03
S.98E-07
6.49E-07
3.33E-06
1.96E-07
1.08E-06
1.37E-06
8.24E-08
4.90E-07
3.73E-07
2.SSE-07
2.06E-06
Total HAP
Emission Rate b,c
(lb/hr) (tpy)
4.74E-06 7.0lE-09
l.69E-04 2.S0E-07
4.06E-03 6.0lE-06
1.38E-06 2.04E-09
1.49E-06 2.21E-09
7.67E-06 1.14E-08
4.SlE-07 6.68E-10
2.48E-06 3.67E-09
3.16E-06 4.68E-09
l.89E-07 2.81E-10
l.13E-06 1.67E-09
8.57E-07 1.27E-09
S.86E-07 8.68E-10
4.74E-06 7.0lE-09
4.26E-03 6.30E-06
a.AP-42 Section 1.4, Natural Gas Combustion (July 1998), Table 1.4-3 for organic HAP and Table 1.4-4
for metal HAP, converted from lb/MMscf to lb/MM Btu using the heating value of 1,020 Btu/scf.
b.Emission Rate (lb/hr)= Emission Factor {lb/MMBtu) * Hourly Heat Input (MM Btu/hr)
c.Emission Rate (tpy) a: Emission Factor (lb/MMBtu) * Annual Heat Input (MM Btu/yr) * (ton/2,000 lb)
Emission Equipment Description,
Emission Unit ID No.;
PRODUCTION/OPERATION DATA
Bin Vent Filter [CD·UH-K3) flowrate
Bin Vent Filter [CO-UH-K8) flowrate
Annual Hours of Operation
Criteria Emissions from U F Resin Additives
Source
Urea Unloadin� Hoooer CES·UH·K3l • OS-35
Urea Unloadine Ho ooer /ES·UH-K8l • 0S-36
UF Resin Additives
Urea Unloading Hopper (ES·UH·K3) OS 35
Urea Unloading Hopper (ES-UH-KB) OS 36
1,200dscfm
1,200dscfm
ZBB hriyr
Control Device
ID
CD·UH·K3
CD•UH•K8
Emission
Factor
(gr/dscf)" llb/hr\
0.01 0.10
0.01 0.10
a. PM/PM1o/PM2 , emission factors based on engineering estimate.
Controlled Emission Rates'·'
PM PM 10 I lt.,vl (lb/hr) I (tnvl I 0.10 I 0.01 I 0.01 0.10 I 0.01
b. Emission Rate (lb/hr)= Emission Factor (gr/dscf) • Maximum Air Flow Rate [dscfm) • [lb/7,000 gr)• [60 min/hr)
(lb/hr)
0.10
0.10
c. Emission Rate (t py l = Emission Factor [gr/dscf) • Maximum Air Flow Rate [dscfm} • (lb/7,000 gr) • (ton/2,000 lbl • (60 min/hr) • (8,760 hr/yr)
Thoughput
12,054,380
13,378,630
PM2_5 l (tnvl
0.01
0.01
Total Urea
hr/yr
25,433,009
288.36
Emission Equipment Description:
Emission Unit ID No.:
PRODUCTION/OPERATION DATA
Bin Vent Filter {C0-11.1) flowrate
Bin Vent Filter {CD-11.2) flowrate
Bin Vent Filter {CD-11.6) flowrate
Annual Hours of Operation
RESl•MIX• Manufacturing
RM3 Extender Storage Silo (ES-11.1)
RM4 Extender Storage Silo (ES•ll.2)
RESl•MIXER• (ES4.6)
800 dscfm
800 dscfm
3,840 dscfm
�781 hr /yr
Criteria Emissions from UF Resin Additives
Emlsslon Control Device Source Factor ID (gr/dscf)• llb/hrl
RM3 Extender StoraRe Silo (ES-11.ll CD-11.1 0.01 O.Q7
RM4 Extender Storage Silo (ES-11.2) CD-11.2 o.oi 0.07
RESI-MIXER• (ES4.6l CD-11.6 0.01 0.33
a.PM/PMw'PM2.s emission factors based on engineering estimate.
Controlled Emission Rates b,,
PM PM10 PM2.s
(tnvl Clb/hrl (tpy) (lb/hr)
0.23 O.o7 0.23 0.07
0.23 0.07 0.23 0.07
1.12 0.33 1.12 0.33
b.Emission Rate (lb/hr)= Emission Factor (gr/dscf) • Maximum Air Flow Rate (dscfm) • (lb/7,000 gr) • (60 min/hr)
(tpy) 0.23
0.23
1.12
c.Emission Rate {tpy) = Emission Factor (gr/dscf] • Maximum Air Flow Rate (dscfm) • (lb/7,000 gr)• [ton/2,000 lb)• (60 min/hr)• (8,760 hr/yr)
Emission Equipment Description:
Emission Unit ID No.:
OPERATION DATA
Circulation Rate:
Total Dissolved Solids:
Drift Factor:
Drew 2105 Concentration•:
Drew 2105% voe•:
Annual Hours of Operation:
Cooling Tower
ES-TlA
7,200 gpm
960 ppm
0.001%
100 ppm
0.64%
8,760 hr/vr
a.Based on the data provided by the manufactuerer.
Emissions Calculations
Pollutant Emission Factor a,b Emission Rate
(lb/gal) (lb/hr) (tpy)
PM 8.0lE-08 0.03 0.15
PM10 --0.03 0.14
PM2 .s --0.03 0.12
voe 5.34E-06 2.31 10.10
a.PM Emission Factor= Density of Water (lb/gal)* Drift Factor(%)• Total Dissolved Solids (ppm)/ 106
voe Emission Factor= Density of Water (lb/gal) • Drew 2105 voe Concentration (ppm)/106 • Drew 21055 % voe(%)
b.PM10 and PM2_5 speciation based on EPA PMCALC speciation.
Reisman and Frisbie values not provided for TDS below 1,000 ppm.
PM10 =94% PM
PM2 .s =78% PM
Emission Equipment Description:
Emission Unit ID No.:
OPERATION DATA
Circulation Rate:
Total Dissolved Solids:
Drift Factor:
Drew 2105 Concentration•
Drew 210s % voe•
Annual Hours of Operation:
Cooling Tower
ES-T3
10,000 gpm
960 ppm
0.001%
100 ppm
0.64%
8,760 hr/vr
a.Based on the data provided by the manufactuerer.
Emissions Calculations
Pollutant Emission Factor a,b Emission Rate
(lb/gal) (lb/hr) (tpy)
PM 8.0lE-08 0.05 0.21
PM 10 --0.05 0.20
PM2.s --0.04 0.16
voe 5.34E-06 3.20 14.03
a.PM Emission Factor= Density of Water (lb/gal)* Drift Factor (%)• Total Dissolved Solids (ppm)/ 106
voe Emission Factor= Density of Water (lb/gal) * Drew 2105 voe Concentration (ppm)/106 * Drew 21055 % voe(%)
b.PM10 and PM2.s speciation based on EPA PMeALe speciation.
Reisman and Frisbie values not provided for TDS below 1,000 ppm.
PM10= 94% PM
78% PM
Emission Unit 01ucripUon:
P1ved Ro1ds (PR·ll
Road Se1menl Data
Road
se-ame-nt Paved/Unpaved
A
B
C
D
Pavt'd
Pavfl'd
Paved
Poved
True• Traffic Del.alls• Potenllal
Lenctti
1ml) Trucks
0 36 Urt-1/Ammonl.a/Re,jn Addmvu
0.38 c,ustk/Methanol
0.40 Spr.ayOry/Ware�•e
0.46 Resin. Miscelbneous
Truck Wel1ht1 A.ve-r.ase Truck ltons) TruckWei.1,ht N1,1mberof
Unloaded loaded (1ons1 TIU<ltSJ
u,ea/Ammonla/Resln Additives 15 40 27.S 506
Caustic 15 40 275 347
Methanol lS 40 2H l,428
�pray Ory 15 40 27S 764
Warehouse 15 40 27.S 520
Resin 15 40 27.S 6,440
Miuelbneous 15 40 27S 520
1. l,uck weight b.asNI on eng.lnffflna: �timate1..
2. Numbe1 of trucks b.ased on rncJneering estimate.
Fleet Mean Emb,lon Futor1
Sesmient W11Jht PM PMao PM._. VMT
fto.,sl (lb/VMT) llbNMn Ub/VMTI
Paved
A 27.5 2.00 0.4, 0.1):)8 364
B 27.S 2.00 0.40 0.098 1.349
C 27.5 2.00 0.40 0.008 l.<ll1
0 27.S 2.00 0.40 0.098 640,
Total Emissions
l. P•ved route emi'Hlon factor is b•scd an Equation 2 of AP--42 Section 13 2.1 (J.anuary 2011):
E = [k x (sl )"' x (w )' u.t ]x ( I 4� )
E • sl.te specific emission h1ct01 (lb/VMT]
Routes
Re1.in 8.ad: g.ate in/Sad, gate out
Resin fronl g.ale In/Front 1,.ate out
Spray Dry 1ate ln/Spcay Ory 1alt'OUl
kesin Back Gate In/Front Gate· out
Route1, Traveled
A B C D t
i I t , t
2
Emlsslons:I
PM PM,.
llb/hrl Uovl llb/hrl ltovl
0.08 0.33 0.02 0.07
0 31 1.22 0.06 0.24
0.23 0.93 0.05 0.19
1.46 5.78 0.29 116
2.09 8.26 0.42 1.65
PMu
Hb/h,l Uovl
o.oo 0.02
0.02 0.06
0.01 0.05
0.07 0.28
0.10 0.41
Ir.• O.Oll (PMI �nide size multipliier for panlde sire nnee �nd uniu,of lnterHt. AP-42. St-ctlOn 13.l.l, Tabte 13.2.1•1.
0.0022 (PMI0)
0.00054 (PM2 SI
sl • 7.4 ro•d surface silt ki•d<ln,: �m tl, based on th,e va\Jefor mun •if>al �td wutet.andfi'h in AP-42 Se-ction 13.2 1. Tible 13.21 3
W = mHn v�hicle wei1h1 (1om-J
P• 140 number of da�in th .ave,.agingperiod with at leutei.2S4mm [O.Olln .of pre(lpitaUon..AP-42 Section 13.2 1, flsure 13 2 1·1
N • 36S number of days. In the avenging period (e.e., 36S fDf' annual�
Note that rain correction f�<tor (1·P/4N)only appl�s to annual, n01 hourfyemlssk>ns.
2. EmissioAs ufculated from emlss.lon facto, times VMT per route. Hourly emission, an:ume 8,760 hours of opera.�