AQ_F_1900077_20170626_EI_Cmb-EI-File

2016 Emissions Inventory Review / Data Tracking Form
Facility Name: Triangle Brick Company - Merry Oaks Facility ID: 1900077
Facility Assigned to: Data Entry: Chatham County
Classification: Stanley Williams Confidential Copy Submitted?
Title V 0
0 YES
NO
Initial Review/Data Entry
0 Enter date received into ED. Date Received: !o ZCo- 20 17
8 Assigned to appropriate individual. Date Assigned: Date Due: /O•/5 :2e�j'7
❑ Paver copy submitted: One copy received with supporting documentation,certification form signed by responsible official,and
appears generally complete;OR
21 Electronic copy submitted: All supporting documentation and certification form(with time/date stamp)signed by responsible
official has been received.
Comments:
Inventory Review
❑ All forms and supporting documentation appear to be complete if paper submission(check ED OS data if electronic).
0 Contact,address,phone number changes entered into I-Beam/Facilities if necessary.
21 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.
0 Check if SCC codes for each OS are accurate and update if needed.
❑ Evaluate"U"sources for significance and address according to policy.
0 Calculations/forms appear to add up correctly.
Wr All compliance issues are being addressed(e.g.Toxics limits,above TV thresholds,large emissions increase/decrease,installation
without a permit).
0 All volatile HAPs/TAPs were included in the VOC total.
0 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.).
0 Review facility comments and address any issues.
❑ Update ED(Data Entry Main)if additional information is required(corrections due date and date received).
7 Check all ED QA/QC reports.
0 Comparison with previous emission inventory must be made and outliers(> 10%)must be investigated and explained.
0 Put inventory review comments and summarize any changes in ED-Data Entry Main"DAQ internal comments".
0 Print and attach the facility total report.
Date Info Requested: Date Info Received: Total Days on Hold:
Date Review Complete: /D-//b Z017 Signature:
Date Submitted to EI Coordinator: /O•//a Zj/7
Date Approved: j0 l 1 17 Initials:

Facility Total CY 2016 Emission Summary Recorded in ED Facility ID #: 1900077
Facility Name: . Triangle Brick Company- Merry Oaks Permit#(s): 06897T10
Green House Gases Pollutants (GHG) Actual Emissions
Tons/Yr
Pollutant CAS
Demini- Change
mus
Not Not N/A
Reported Reported.
CO2 equivalent(sum of individual GHG pollutant emission No GHGs
times their 1995 IPCC Global Warming Potential (GWP), Reported
converted to metric tons)
Criteria Pollutants Actual Emissions
(Tons/Year)
Pollutant CAS CY 2016 CY 2015 Demini- %
from ED from Fees mus Change
CO CO 42.28 40.57 0.5 4.2%
NOx NOx 9.31 9.07 0.5 2.6%
PM(TSP) TSP 64.92 34.20 0.5 89.8%
PM10 PM10 47.96 25.35 0.5 89.2%
M2.5 ' PM2.5 34.43 25.35 0.5 35.8%
S02 S02 4.58 4.85 0.5
VOC VOC 6.12 5.29 0.5
Hazardous Air Pollutants (HA-Ps) Actual Emissions
and/or Toxic Air Pollutants (TAPS) (Pounds/Year)
Pollutant CAS
CY 2016 CY 2015 Demini- %
from ED from Fees mus Change
Antimony & Compounds (total mass, inc elemental SB) 9.33 8.95 10.0 4.2%
Antimony Metal - (Component of SBC) 7440-36-0 Not 0.067430 10.0 N/A
Reported
Antimony Unlisted Compounds- Specify Compounc SBC-Other 9.33 8.88 10.0 5.1%
(Component of SBC)
Arsenic.& Compounds (total mass of elemental AS, arsine and 3.35 3.22 0.01 14.0%
all inorganic compounds)
Arsenic Metal, elemental, unreacted (Component of 7440-38-2 Not 0.031810 0.01 N/A
ASC) Reported
„ .=c."Senic Unlisted Compounds - Specify Compound ASC-Other 3.35 3.19 0.01 5.1%
(Component of ASC)
10/11/2017 Pagel of 4

Facility Total CY 2016 Emission Summary Recorded in ED Facility ID #: 1900077
Facility Name: Triangle Brick Company-Merry Oaks Permit#(s): 06897TI O
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPs) (Pounds/Year)
Pollutant CAS CY 2016 CY 2015 Demini- %
from ED from Fees mus Change
Beryllium & compounds (Total mass) 0.061440 0.064430 L0 I -4.6%
Beryllium Metal (unreacted) (Component of BEC) 7440-41-7 0.061420 0.064410 1.0 -4.6%
Beryllium Unlisted Compounds- Specify Compounc BEC-Other 0.000020 0.000020 1.0 N/A
(Component of BEC)
Cadmium.& compounds (total mass includes elemental metal) 0.844370 0.829480 0.1 11.8%
Cadmium Metal, elemental, unreacted(Component( 7440-43-9 0.844370 0.829480 0.1 1.8%
CDC)
Chromium-All/Total(includes Chromium (VI) categories, 3.06 3.07 0.1 I -0.3%
metal and others)
Chromium (VI)Non-Specific Unlisted Compounds - NSCR6-other 0.002620 0.033000 0.01 -92..1%
Specify Compound(Component of NSCR6 & CRC)
Chromium Unlisted Compounds - Specify Compoun CRC-Other 3.06 3.03 0.1 0.7%
(Component of CRC)
Chromium (VI)Non-Specific Compounds, as Chrom(VI) 0.002620 0.033000 0.01
( Ponent CRC) 1-92.1%
I
(Component
Chromium (VI)Non-Specific Unlisted Compounds- NSCR6-other 0.002620 0.033000 0.01 1 -92.1'%
Specify Compound(Component of NSCR6 & CRC)
Cobalt& compounds 0.624580 0.598880 1.0 14.3%
Cobalt Unlisted Compounds - Specify Compound COC-other 0.624580 0.598880 1.0 4.3%
(Component of COC)
Lead& compounds 21.94 21.05 1.0 4.2%
Lead Unlisted Compounds- Specify Compound PBC-Other 21.94 21.05 10.0 4.20/
(Component of PBC)
Manganese & compounds 12.37 11.89 10.0 14.0%
Manganese Unlisted Compounds- Specify Compout MNC-other 12.37 11.89 10.0 4.1%
(Component of MNC)
Mercury & Compounds-all total mass includes Hg Vapor 1.46 1.41 0.001 13.5%
r
Mercury, vapor(Component of HGC) 7439-97-6 1.46 1.41 0.001 3.99/c
Nickel& Compounds, sum total mass includes elemental 1.88 2.11 1.0 10.9%
10/11/2017 Page 2 of 4

Facility Total CY 2016 Emission Summary Recorded in ED Facility ID #: 1900077
Facility Name: Triangle Brick Company-Merit Permit#(s): 06897TIO
,`iazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants,(TAPs) (Pounds/Year)
Pollutant CAS CY 2016 CY 2015 Demini- %
from ED from Fees mus Change
Nickel metal (Component of NIC) 7440-02-0 1.88 2.11 1.0 -1.1.0%
Polycyclic Organic Matter(Specific Compounds from OAQPS 9.51 9.12 1.0 14.3%
for Tip
Naphthalene (Component of 83329/POMTV) 91-20-3 9.51 9.12 1.0 4.3%
Acetaldehyde 75-07-0 0.000030 0.000030 10.0 N/A
Acrolein 107-02-8 0.000030 0.000030 10.0 N/A
Ammonia(as NH3) 7664-41-7 5.99 5.55 100.0 7.9%
Benzene 71-43-2 424.09 406.64 1.0 4.3%
Carbon disulfide 75-15-0 6.29 6.03 10.0 4.3%
Chlorine 7782-50-5 190.11 182.28 100.0 4.3%
DEHP (Di(2-ethylhexyl)phthalate) 117-81-7 292.47 280.44 10.0 4.3%
"ibutylphthalate 84-74-2 20.47 19.63 100.0 4.3%
])ichlorobenzene(p), 1,4- 106-46-7 7.02 6.73 1.0 4.3%
Ethyl benzene 100-41-4 6.43 6.17 100.0 4.3%
Ethyl chloride (chloroethane) 75-00-3 83.35 79.92 10.0 4.3%
Fluorides (sum of all fluoride compounds as mass of 16984-48-8 58,141.13 62,817.60 10.0 F-7.4%
ion)
Formaldehyde 50-00-0 39.19 37.91 10.0 3.4%
Hexane, n- 110-54-3 3.37 3.12 100.0 7.9%
Hydrogen chloride (hydrochloric acid) 7647-01-0 16,551.00 35,584.67 100.0 -53.5%
Hydrogen fluoride (hydrofluoric acid as mass of HF) 7664-39-3 36,459.00 58,273.92 100.0 -37.4%
(Component of 16984488/Fluorides)
MEK (methyl ethyl ketone, 2-butanone) 78-93-3 32.17 30.85 100.0 4.3%
Methyl chloride (chloromethane) 74-87-3 97.98 93.95 1.0. 4.3%
Methyl chloroform 71-55-6 0.687300 0.659030 100.0 4:3%
Methyl iodide (iodomethane) 74-88-4 13.60 13.04 10.0 4.3%
„JBK (methyl isobutyl ketone) 108-10-1 12.43 11.92 10.0 4.3%
Perchloroethylene (tetrachloroethylene) 127-18-4 0.409460 0.392610 100.0 4.3%
10/11/2017 Page 3 of 4

Facility Total CY 2016 Emission Summary Recorded in ED Facility ID #: 1900077
Facility Name: Triangle Brick Company-Merry Oaks Permit#(s): 06897T 10
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPS) (Pounds/Year)
Pollutant CAS CY 2016 CY 2015 Demini- %
from ED from Fees mus Change
Phenol 108-95-2 12.58 12.06 100.0 4.3%
- Polycyciic-Organic-Matter(IncPAH;dioxins,-etc.--N -pOM- - -Not- - 0.042390 1.0 NIA--
& AP 42 historic) Reported
Selenium Compounds SEC 6.26 6.00 10.0 4.3%
Styrene 100-42-5 2.92 2.80 100.0 4.3%
Toluene 108-88-3 23.40 22.44 100.0 4.3%
Xylene (mixed isomers) 1330-20-7 9.80 9.46 100.0 3.6%
Xylene, o- 95-47-6 8.48 8.07 100.0 5.1%
Largest Individual HAP Rydrogen fluoride (hydrofluoric acid a. 36,459.00 lbs
mass of HF) (Component of
Total HAP Emissions 54,335.75 lbs
Largest Individual CAP PM10 47.96 tons
Total CAP Emissions 110.25 tons
Total TAP Emissions 112,230.66 lbs
Total Aggregate 165.92 tons
Emissions
DAQ's Comments Relzarding Inventory
Only Kiln 3 operated during 2016 with a total brick production of 146,235 tons of brick,with 96,665 tons of that being produced
without using the DLA(without controls)and 49,570 tons produced with using the DLA. Emission factors established with the
September 2016 stack test were used for the controlled portion(49,570 tons)of the inventory and AP-42 for the uncontrolled portior
The percent change in chromium(VI)and.nickel metal are due to no distillate oil being burned in the kilns. The VOC percent chans
is due to the increased throughput of tanks No.2,3,and 4. The percent change in HCL and HF are due to the facility not using the
DLA control device on Kiln 3(only kiln operated in 2016)for the majority of the year. The percent change in particulate matter
emissions are influenced by the lack of use of the control device plus primarily only accounting for filterable particulate matter in th,
past and not total particulate matter. PM-2.5 does not have an emission factor for filterable pm and the best approximation for total
PM-2.5 was to use the AP-42 emission factors for condensible inorganic and organic PM.
10/11/2017 Page 4 of 4

Triangle Brick
.CW1
6523 NC Highway 55
Durham, NC 27713
June 27,2017 Durham: [phone]
Raleigh: [phone]
Toll Free:800-672-8547
Fax:[phone] z
n
North Carolina Department of Environmental Quality
Raleigh Regional Office C
Air Quality Section , C °
3800 Barrett Drive. 2
Raleigh,North Carolina 27609
t o• co c
Attention: Air Emission Inventory to o
V �
Reference: Submittal of 2016 Air Emission Inventory ,o
Certification Form and Supporting Emission Calculations
Triangle Brick Company—Merry Oaks
Dear Sirs:
Enclosed please fmd the 2016 Emission Inventory Certification Forms for Triangle Brick Company's
Merry Oaks, North Carolina facility. The actual emission inventories were submitted using NCDAQ's
AERO system. In addition we are submitting supporting emission calculations for the facility.
Annual emissions were estimated using emission factors developed during a United States Environmental
Protection Agency/Brick Association of North Carolina sponsored source test at our Merry Oaks facility,
emission factors contained the AP-42 Section 11.3 "Brick and Related Clay Products," and AP-42 fuel
combustion emission factors. Since the Dry Limestone Absorber(DLA)has been in continuous operation
since August, Hydrogen chloride and hydrogen fluoride emissions are partitioned into controlled and
uncontrolled emissions. Uncontrolled emission factors are based on testing that was done at the facility
prior to the installation of the DLA (October 1995). Controlled emissions were estimated using emission
factors based on testing that was done at the facility in February 2017. Greenhouse gas emissions are not
included since it is not mandatory and more importantly emission factors from brick plants are not readily
available for these pollutants. Emissions of these pollutants will be included when required.
If you have any questions, please do not hesitate to contact me at [phone] or Michael Cantoni at
[phone].
Sincerely,
TRIANGLE BRICK COMPANY
Howard P. Brown,Jr.
President and CEO
cc: Ricky Merritt, Director of Engineering

COPY of RECORD Date Submitted: 6/26/2017 17:01 :50
Lz Inventory rertification Form(Title V)
C —acility 1*gne: Triangle Brick Company—Merry Oaks Facility ED : 1900077
294 King Rd Permit: 06897
Moncure,NC 27559 County : Chatham
c DAQ Region : RRO
�-- North Carolina Department of Environment and Natural Resources
Division of Air Quality
-' Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
_ R
zThese 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 Howard Brown.Jr.
This person or one that meets the definition below must sign this certification form.
The official submitting the information must certify that he/she complies with the requirements as specified in Title 15A
NCAC 2Q.0520(b)which references and follows the federal definition.40 CFR Part 70.2 defines a responsible as meaning one
of the following:
1.For a corporation: a president,secretary,treasurer,or vice—president of the corporation in charge of a principal
business function,or any other person who performs similar policy or decision making functions for the overall
operation of one or more manufacturing,production,or operating facilities applying for a or subject to a permit and
either
i.the facilities employ more than 250 persons or have gross annual sales or expenditures exceeding$25
million(in second quarter 1980 dollars);or
ii. the delegation of authority to such representatives is approved in advance by the permitting authority;
2. For partnership or sole propietorship;a general partner or the proprietor,respectively;
3. for a muncipality, state,federal,or other public agency includes the chief executive officer having responsibility for the
overall operations of a principal geographic unit of the agency(e.g.,a Regional Administrator of EPA).
CERTIFICATION TAT
(Importanta Legally Rcsponsible
certify that I am the responsible official for this facility,as described above,and hereby certify that the information contained
in this air emissions report, including attached calculations and documentation,is true,accurate and complete. (Subject to legal
enalities of up to$25,000 per occurrence and possible imprisonment as outlined in G.S.§143-215.3(a)(2))
Responsible Official's Signature Below use blue ink): Date Signed: (r, I
Printed Name: Howard Brown,Jr.
Si nature:
This form applies to Title V facilities. If this facility is not classified as Title V,please telephone your regional office Emission
Inventory contact at once for proper forms.
Email address of Responsible Official: [e-mail]
Information on this Form cannot be held confidential
COPY of RECORD Date Submitted: 6/26/2017 17:01:50 1

n
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C ,71
Z <
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2016 AIR EMISSIONS INVENTORY
TRIANGLE BRICK COMPANY
MERRY OAKS, NORTH CAROLINA
FACILITY ID: 1900077
PREPARED FOR:
Triangle Brick Company
Durham,North Carolina
PREPARED BY:
ERM NC, Inc.
4140 Parklake Avenue, Suite 110
Raleigh,North Carolina 27612
June 2017

AERO EMISSION INVENTORY PRINTOUT
TRIANGLE BRICK COMPANY-MERRY OAKS

COPY of RECORD Date Submitted: 6/26/2017 17:01 :50
As entered in AERO
Facility Name: Triangle Brick Company—Merry Oaks Facility ID : 1900077
294 King Rd Permit: 06897
Moncure,NC 27559 County: Chatham
DAQ Region : RRO
Listing of Emission Sources and Control Devices on Permit. See instructions
*ES ID on DES Description GCS ID *CS Description CD ID's
Air Permit
CG-1 Clay Feeder
CG-10 Finish Screen[NSPS 000]
CG-11 IFinish Screen[NSPS 000]
CG-12 Finish Screen [NSPS 000]
CG-13 Belt to Storage Bins[NSPS 000]
CG-14 Belt over Storage Bins [NSPS
000]
CG-15 Feeders under Bins[NSPS 000]
CG-16 Feeders under Bins[NSPS 000]
rG-17 Feeders under Bins[NSPS 000]
G-18 Feeders under Bins[NSPS 000]
CG-19 Feeders under Bins[NSPS 000]
CG-2 Belt to Scalping Screen[NSPS
000]
CG-20 Feeders under Bins [NSPS 000]
CG-22 Feeders under Bins [NSPS 000]
CG-23 Feeders under Bins [NSPS 000]
CG-24 Feeders under Bins [NSPS 000]
CG-25 Conveyor from Storage Bin
[NSPS 000]
CG-26 Conveyor from Storage Bin
[NSPS 000]
CG-27 Conveyor to Pug Mill [NSPS
000]
CG-28 Conveyor to Pug Mill [NSPS
000]
CG-29 Clay Feeder
CG-3 Scalping Screen[NSPS 000]
CG-30 Belt to Scalping Screen[NSPS
000]
;G-31 Scalping Screen[NSPS 000]
CG-32 Return Belt from Oversize Screen
[NSPS 000]
2

CG-33 Belt to Hammermill[NSPS 000]
CG-34 Hammermill[NSPS 000]
`-;G-35 Belt to Screens[NSPS 000]
CG-36 Belt over Finish Screens [NSPS
000]
CG-37 Finish Screen[NSPS 000]
CG-38 Finish Screen[NSPS 000]
CG-39 Finish Screen[NSPS 000]
CG-4 Return Belt for Oversizes from
Screens [NSPS 000]
CG-40 Finish Screen[NSPS 000]
CG-41 Belt to Storage Bins [NSPS 000]
CG-42 Belt over Storage Bins [NSPS
000]
CG-43 Feeders under Bins [NSPS 000]
CG-44 Feeders under Bins [NSPS 000]
CG-45 Feeders under Bins [NSPS 000]
CG-46 Feeders under Bins [NSPS 000]
CG-47 Feeders under Bins [NSPS 000]
CG-48 Conveyor from Storage Bin
[NSPS 000]
IC7G-49 Conveyor to Pug Mill[NSPS
000]
'G-5 Belt to Hammermill[NSPS 000]
CG-6 Hammermill [NSPS 000]
CG-7 Belt to Screens [NSPS 000]
CG-8 Belt over Finish Screen[NSPS
000]
CG-9 Finish Screen[NSPS 0001
IS-1.1 conveyor to loam/sawdust system
IS-1.2 conveyor to loam/sawdust system
IS-2.1 loam screen
IS-2.2 loam screen
IS-3.1 loam crusher
IS-3.2 loam crusher
IS-4.1 oversize return conveyor from
loam screen
IS-4.2 oversize return conveyor from
loam screen
IS-5.1 oversize loam return shoot
IS-5.2 oversize loam return shoot
IS-6.1 sawdust screen
S-6.2 sawdust screen
iS-7.1 conveyor to storage bin
IS-7.2 Iconveyor to storage bin
3

IS-8.1 oversize conveyor from sawdust
screen
�, oversize conveyor from sawdust
—8.2 screen
IS—CD-50 Conveyor from extruder to pug
Mill
IS—CL1 Cosmetic loam operation area
IS—CL2 Cosmetic loam operation area
IS—EXTRl lExtrusion and setting line
IS—EXTR2 Extrusion and setting line
IS—LS 1 loam/sawdust feeder
IS—LS2 loam/sawdust feeder
IS—Tankl 24,000 gallon No. 6 fuel oil
storage tank
IS—Tank2 24,000 gallon No.2 fuel oil
storage tank
IS—Tank3 24,000 gallon No.2 fuel oil
storage tank
IS—Tank4 24,000 gallon highway diesel fuel
storage tank
IS—Tanks 24,000 gallon additive"A" storage
tank
IS—Tank6 3,000 gallon gasoline storage tank
Kiln 1—Natural gas/No.2 fuel
oil/No. 6 fuel oil—fired brick
tunnel kiln(14.5 tons per hour
K-1 maximum brick production
capacity,21.4 million Btu per hour
maximum heat input rate) [2D
1109 Case by Case MACT]
Kiln 2—Natural gas/No.2 fuel
oil/No. 6 fuel oil—fired brick
tunnel kiln(14.5 tons per hour
K-2 maximum brick production
capacity,21.4 million Btu per hour
maximum heat input rate) [2D
1109 Case by Case MACT]
Kiln 3—Natural gas/No.2 fuel
oil/No. 6 fuel oil—fired brick
tunnel kiln(29 tons per hour
K-3 maximum brick production
capacity,42.8 million Btu per hour
maximum heat input rate) [21)
.1109 Case by Case MACT]
PC-1 Shale Feeder
pC-2 Scalp Screen[NSPS 000]
'C-3 Jaw Crusher[NSPS 000]
PC-4 Conveyor under PC-2 and PC-3
[NSPS 000]
4

PC-5 Cross over Conveyor[NSPS
000]
Shuttle Conveyor(Enclosed in
—6 Clay Storage Building) [NSPS
000]
Natural gas—fired rotary coatings
SD-1 dryer(0.3 million Btu per hour
maximum heat input) [NSPS
UUU]
5

COPY of RECORD Date Submitted: 6/26/2017 17:01 :50
As entered in AERO
Facility Name: Triangle Brick Company-Merry Oaks Facility ID : 1900077
294 King Rd Permit: 06897
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
Emission Source & Operating Scenario List- See Instructions
'DES Group ID DES ID *OS ID *OS Description
PC-1,PC-2,PC-3, Primary Crusher and associated
G-72 PC-4,PC-5,PC-6 15 crushers
CG-1,CG-10,CG-11,
CG-12,CG-13,CG-14,
CG-15,CG-16,CG-17,
CG-18,CG-19,CG-2,
CG-20,CG-22,CG-23,
CG-24,CG-25,CG-26,
CG-27,CG-28,CG-29,
CG-3,CG-30,CG-31, Final Crushing and Grinding
�' �' CG-32,CG-33,CG-34, 16 Operation
CG-35,CG-36,CG-37,
CG-38,CG-39,CG-4,
CG-40,CG-41,CG-42,
CG-43,CG-44,CG-45,
CG-46,CG-47,CG-48,
CG-49,CG-5,CG-6,
CG-7,CG-8,CG-9
IS-1.1 NONE NONE
IS-1.2 NONE NONE
IS-2.1 NONE NONE
IS-2.2 NONE NONE
IS-3.1 NONE NONE
IS-3.2 NONE NONE
IS-4.1 NONE NONE
IS-4.2 NONE NONE
IS-5.1 NONE NONE
IS-5.2 NONE NONE
IS-6.1 NONE NONE
IS-6.2 NONE NONE
IS-7.1 NONE NONE
IS-7.2 NONE NONE
IS-8.1 NONE NONE
IS-8.2 NONE NONE
IS-CD-50 NONE NONE
IS-CL1 NONE NONE
6

IS—CL2 NONE NONE
IS—EXTRI NONE NONE
IS—EXTR2 NONE NONE
IS—LS 1 NONE NONE
IS—LS2 NONE NONE
12 24,000 gallon No. 6 fuel oil storage
IS—Tankl tank
21 No. 6 fuel oil tank—standing
emissions
IS—Tank2 22 No.2 fuel oil tank—standing and
working emissions
IS—Tank3 23 No.2 fuel oil tank—standing and
working emissions
IS—Tank4 24 No.2 fuel oil tank—standing and
working emissions
IS—Tanks 13 24,000 gallon Additive A. storage
tank
IS—Tank6 14 3,000 gallon gasoline storage tank
1 Natural gas combustion—primary
2 Distillate fuel and NG
K-1 combustion—secondary
17 Residual Oil and NG
combustion—tertiary
3 Natural gas combustion—primary
4 Distillate fuel and NG
K-2 combustion—secondary
18 Residual Oil and NG
combustion—tertiary
5 NG combustion—primary
6 Distillate and Natural gas
K-3 combustion—secondary
19 Residual Oil and NG
combustion—tertiary
SD-1 20 Natural Gas Combustion
7

COPY of RECORD Date Submitted: 6/26/2017 17:01 :50
As entered in AERO
Facility Name: Triangle Brick Company—Merry Oaks Facility ID : 1900077
294 King Rd Permit: 06897
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
1. Emission Source ID(from permit)or Group G-72 consisting of PC-1,PC-2,PC-3,PC-4,PC-5,PC-6
Emission Source Group ID
2. Emission Source Description: Primary Crusher and associated crushers
3. Operating Scenario ID/Description: OS— 15/Primary Crusher and associated crushers
4. SCC Number/Description: 30500340Brick Manufacture—Material Prep;Primary Crusher
5. Throughput/units in 2016: 192414 TON/yr
(e.g.production or fuel use):
6. Fuel Information (if fuel is used) ro
Sulfur ro Ash I Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point RP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
EP—FUG FUGITIVE(NO 1 72 Area= 1 ERP for Fugitive
STACK) sources
8

v
Operating Scenario: OS— 15 Emission Source/Group ID: G-72
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
Sours per Day ( 8 ) Days per Week ( 4 ) Weeks per Year ( 28 )
11.Typical Start&End Times For Operating Scenario: Start: 800 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 17% 330�o line—Aug. �arch,—Mayept.—Nov. 17��u
2016 016 016� 016
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po�QS Code Pollutants Method Code (Net after Factor Ef Control
Pollutantss
(Tons/Year) (See Instructions) all controls)
2016
CO CO 08
NOz NOz 08
TSP TSP 5.68 08 0.059
PM10 PM10 5.68 08 0.059
PM2.5 PM2.5 5.68 08 0.059
S02 S02 08
VOC VOC 08
HAP/TAP CAS Emissions Emission Control
Pollutants (in HAP/TAPS Estimation Emission
(see instructions) Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2016
9

COPY of RECORD Date Submitted: 6/26/2017 17:01 :50
As entered in AFRO
Facility Name: Triangle Brick Company-Merry Oaks Facility ID : 1900077
294 King Rd Permit: 06897
Moncure,NC 27559 County: Chatham
DAQ Region :RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory-Calendar Year 2016
1. Emission Source ID(from permit)or Group G-73 consisting of CG-1,CG-10,CG-11,CG-12,CG-13,CG-14,
Emission Source Group ID CG-15,CG-16,CG-17,CG-18,CG-19,CG-2,CG-20,CG-22,CG-23,
CG-24,CG-25,CG-26,CG-27,CG-28,CG-29,CG-3,CG-30,CG-31,
CG-32,CG-33,CG-34,CG-35,CG-36,CG-37,CG-38,CG-39,CG-4,
CG-40,CG-41,CG-42,CG-43,CG-44,CG-45,CG-46,CG-47,CG-48,
CG-49,CG-5,CG-6,CG-7,CG-8,CG-9
2. Emission Source Description: Final Crushing and Grinding Operation
3. Operating Scenario ID/Description: OS- 16/Final Crushing and Grinding Operation
4. SCC Number/Description: 30500302/Brick Manufacture-Material Prep;Raw Material Grinding
Screening
5. Throughput/units in 2016: 192414 TON/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS-ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point RP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-FUG FUGITIVE(NO 1 72 Area= 1 ERP for Fugitive
STACK) sources
10

Operating Scenario: OS— 16 Emission Source/Group ID: G-73
_ 10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
Sours per Day ( 8 ) Days per Week ( 5 ) Weeks per Year ( 28 )
11.Typical Start&End Times For Operating Scenario: Start: 800 End: 1600
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 15% arch—May 35% une—Aug. 35% Sept.—Nov. 15%
016 016 016 016
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission
Pollutants Pollutants Method Code (Net after Factor Ef Control
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission
Pollutants
Code Pollutants Method Code (Net after Factor Ef Control
(Tons/Year) (See Instructions) all controls)
2016
CO CO 08
NOx NOx 08
TSP TSP 2.41 08 0.025
PM10 PM10 0.22 08 0.0023
PM2.5 PM2.5 0.22 08 0.0023
S02 S02 08
VOC VOC 08
HAP/TAP CAS Emissions Emission Control
Pollutants (In HAP/TAPS Estimation Emission
EF Control
(see instructions) Efficiency
Alphabetical Order Method Code Factor
ounds/Year
P ) (P ) See Instructions) (Net after all controls)
2016
11

C,10 1S0-r Q� i
COPY of RECORD Date Submitted: 6/26/2017 17:01 :50
As entered in AERO
Facility Name: Triangle Brick Company—Merry Oaks Facility ID : 1900077
294 King Rd Permit: 06897
Moncure,NC 27559 County : Chatham
DAQ Region :RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
1. Emission Source ID(from permit)or IS—Tankl
Emission Source Group ID
2. Emission Source Description: 24,000 gallon No. 6 fuel oil storage tank
3. Operating Scenario ID/Description: OS— 12/24,000 gallon No.6 fuel oil storage tank
4. SCC Number/Description: 39090006/Fuel Storage—Fixed Roof Tanks;Oil No. 6: Working Loss
5. Throughput/units in 2016:
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) ro
Sulfur ro Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS-1 1) CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
EP—FUG FUGITIVE(NO 1 72 Area= 1 ERP for Fugitive
STACK) sources
12

Operating Scenario: OS— 12 Emission Source/Group ID:IS—Tankl
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
fours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec ° y ° une—Aug. ° Sept.—Nov. °
2016 25/6 �arch—Ma
16 25/0 �016 25/0 016 25/o
13. Actual Emissions per Pollutant Listed
Attach calculations,and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po� Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2016
CO CO 08
NOz NOz 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP Emissions Emission Control
CAS
Pollutants (in HAP/TAPS Estimation Emission
(see instructions) Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2016
13

COPY of RECORD Date Submitted: 6/26/2017 17:01 :50
As entered in AERO
Facility Name: Triangle Brick Company—Merry Oaks Facility ID : 1900077
294 King Rd Permit: 06897
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
1. Emission Source ID(from permit)or IS—Tankl
Emission Source Group ID
2. Emission Source Description: 24,000 gallon No. 6 fuel oil storage tank
3. Operating Scenario ID/Description: OS —21/No. 6 fuel oil tank—standing emissions
4. SCC Number/Description: 3909000 1/Fuel Storage—Fixed Roof Tanks ;Residual Oil: Breathing Loss
5. Throughput/units in 2016: 0.01 GAL/yr t0��-
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) ro
Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
(as listed inpermit)
9.Emission Release Point RP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
EP—FUG FUGITIVE(NO 1 72 Area= 1 ERP for Fugitive
STACK) sources
14

Operating Scenario: OS—21 Emission Source/Group ID:IS—Tankl
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
[ours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 250�o 250�o11, ne—Aug. 250�o �016
ept.—Nov. 25%
2016 �arch—May ,
16 16
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency
Emission
Po`�QS) Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2016
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP CAS Emissions Emission Control
Pollutants (In HAP/TAPS Estimation Efficient Emission EF Control
(see instructions) Method Code y Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2016
15

COPY of RECORD Date Submitted: 6/26/2017 17:01 :50
As entered in AERO
Facility Name: Triangle Brick Company—Merry Oaks Facility ID : 1900077
294 King Rd Permit: 06897
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
1. Emission Source H)(from permit)or IS—Tank2
Emission Source Group ID
2. Emission Source Description: 24,000 gallon No.2 fuel oil storage tank
3. Operating Scenario ED/Description: OS—22/No. 2 fuel oil tank—standing and working emissions
4. SCC Number/Description: 39090003/Fuel Storage—Fixed Roof Tanks ; Distillate Oil(No.2): Breathing
Loss
5. Throughput/units in 2016: 155000 GAL/yr
(e.g.production or fuel use):
Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
EP—FUG FUGITIVE(NO 1 72 Area= 1 ERP for Fugitive
STACK) sources
16

Operating Scenario: OS—22 Emission Source/Group ID:IS—Tank2
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
ours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu rh ut:
an—Feb +Dec 25% arch—May 250/0 une—Aug. 25% �01
ept.—Nov. 250/o
016 016 2016 6
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year (See Instructions) all controls
2016
Criteria Emissions— Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission Ef Control
Pollutants Code Pollutants Method Code (Net after Factor
(Tons/Year) (See Instructions) all controls)
2016
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC —9' 08
HAP/TAP CAS Emissions Emission Control
Pollutants (in HAP/TAPS Estimation Efficiency Emission EF Control
Alphabetical Order) (see instructions) (Pounds/Year) Method Code (Net after all controls) Factor
See Instructions
2016
17

COPY of RECORD Date Submitted: 6/26/2017 17:01 :50
As entered in AFRO
Facility Name: Triangle Brick Company—Merry Oaks Facility ID : 1900077
294 King Rd Permit: 06897
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
1. Emission Source ID(from permit)or IS—Tank3
Emission Source Group ID
2. Emission Source Description: 24,000 gallon No.2 fuel oil storage tank
3. Operating Scenario ID/Description: OS—23/No.2 fuel oil tank—standing and working emissions
4. SCC Number/Description: 39090003/Fuel Storage—Fixed Roof Tanks;Distillate Oil(No.2): Breathing
Loss
5. Throughput/units in 2016: 15500 GAL/yr
(e.g.production or fuel use):
Fuel Information (if fuel is used) ro
Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point RP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
FEP—FUG FUGITIVE(NO 1 72 Area= 1 ERP for Fugitive
STACK) sources
18

Operating Scenario: OS—23 Emission Source/Group ID:IS—Tank3
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
-Tours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% M 25% �016
une—Aug. 25% ept.—Nov. 25%
016 �arch— a�'
16 �016
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po�QS Code Pollutants Method Code (Net after Factor Ef Control
Pollutantss
(Tons/Year) (See Instructions) all controls)
2016
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC -e-aa 08 ac -54:2 3 i
HAP/TAP CAS Emissions Emission Control
Pollutants (in E AP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2016
19

COPY of RECORD Date Submitted: 6/26/2017 17:01 :50
As entered in AERO
Facility Name: Triangle Brick Company—Merry Oaks Facility ID : 1900077
294 King Rd Permit: 06897
Moncure,NC 27559 County : Chatham
DAQ Region :RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
1. Emission Source ID(from permit)or IS—Tank4
Emission Source Group ID
2. Emission Source Description: 24,000 gallon highway diesel fuel storage tank
3. Operating Scenario ID/Description: OS—24/No.2 fuel oil tank—standing and working emissions
4. SCC Number/Description: 39090003/Fuel Storage—Fixed Roof Tanks ;Distillate Oil(No.2): Breathing
Loss
5. Throughput/units in 2016: 216397 GAL/yr
(e.g.production or fuel use):
Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point RP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
EP—FUG FUGITIVE(NO 1 72 Area= 1 ERP for Fugitive
STACK) sources
20

Operating Scenario: OS —24 Emission Source/Group ID: IS—Tank4
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
[ours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25o�a M 25% une—Aug. 25% Sept.—Nov. 25%
016 �arch— ay
16 2016 016
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission Ef Control
Pollutants Code Pollutants Method Code (Net after Factor
(Tons/Year) (See Instructions) all controls)
2016
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 0.-37 i 08
HAP/TAP CAS Emissions Emission Control
Pollutants (In HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2016
o i L vv e,
21

COPY of RECORD Date Submitted: 6/26/2017 17:01 :50
As entered in AERO
Facility Name: Triangle Brick Company—Merry Oaks Facility ID : 1900077
294 King Rd Permit: 06897
Moncure,NC 27559 County : Chatham
DAQ Region :RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
1. Emission Source ID(from permit)or IS—Tank5
Emission Source Group ID
2. Emission Source Description: 24,000 gallon additive"A" storage tank
3. Operating Scenario ED/Description: OS— 13/24,000 gallon Additive A. storage tank
4. SCC Number/Description: 40714698/Fixed Roof Tanks—Miscellaneous ; Specify In Comments: Working
Loss
5. Throughput/units in 2016: 96608 GAL/yr
(e.g.production or fuel use):
Fuel Information (If fuel is used) ro
Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
FEP—FUG FUGITIVE(NO 1 72 Area— 1 ERP for Fugitive
STACK) sources
22

Operating Scenario: OS— 13 Emission Source/Group ID: IS—Tank5
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
[ours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% 25% une—Aug. 25% �016
ept.—Nov. 25%
016 �arch—May
16 2016
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
(Tons/Year) See Instructions all controls
2016
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po�QS Code Pollutants Method Code (Net after Factor F,f Control
Pollutantss (Tons/Year) (See Instructions) all controls)
2016
CO CO 08
NOz NOz 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 4,4T,0+7 e 08 0.0c��l�'AZ�t
HAP/TAP Emissions Emission Control
Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Yeaz) (Net after all controls)
See Instructions
2016
22

COPY of RECORD Date Submitted: 6/26/2017 17:01 :50
As entered in AERO
Facility Name: Triangle Brick Company—Merry Oaks Facility ID : 1900077
294 King Rd Permit: 06897
Moncure,NC 27559 County : Chatham
DAQ Region :RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
1. Emission Source ID(from permit)or IS—Tank6
Emission Source Group ID
2. Emission Source Description: 3,000 gallon gasoline storage tank
3. Operating Scenario ED/Description: OS— 14/3,000 gallon gasoline storage tank
4. SCC Number/Description: 39090004/Fuel Storage—Fixed Roof Tanks;Distillate Oil(No.2): Working
Loss
5. Throughput/units in 2016: 7741 GAL/yr
(e.g.production or fuel use):
Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
EP—FUG FUGITIVE(NO 1 72 —[--Area= 1 ERP for Fugitive
STACK sources
24

Operating Scenario: OS— 14 Emission Source/Group ID: IS—Tank6
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
[ours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% M 25% une—:lug. 25% ept.—Nov. 25%
016 �arch— ay
16 �016 �016
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po�QS Code Pollutants Method Code (Net after Factor Ef Control
Pollutantss (Tons/Year) (See Instructions) all controls)
2016
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 0.17 08 42e>+6
HAP/TAP CAS Emissions Emission Control
Pollutants (In HAP/TAPS Estimation EfficiencyEmission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2016
25

COPY of RECORD Date Submitted: 6/26/2017 17:01 :50
As entered in AERO
Facility Name: Triangle Brick Company—Merry Oaks Facility ED : 1900077
294 King Rd Permit: 06897
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
1. Emission Source ED(from permit)or K-1
Emission Source Group ID
2. Emission Source Description: Kiln 1—Natural gas/No.2 fuel oil/No. 6 fuel oil—fired brick tunnel kiln(14.5
tons per hour maximum brick production capacity,21.4 million Btu per hour
maximum heat input rate) [2D.1109 Case by C
3. Operating Scenario ED/Description: OS— 1/Natural gas combustion—primary
4. SCC Number/Description: 30500335/Brick Manufacture—Curing Firing;Curing and Firing: Dual
Fuel—fired Kiln,Other Type
Throughput/units in 2016: 1871000 FT3/yr
.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ED CD ID Control Device Description
as listed inpermit)
I I I i 1
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines :
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
lk-1 VERTICAL STACK 57.5 4 488 39.8 30008.49 ERP for Kiln 1
26

Operating Scenario: OS— 1 Emission Source/Group ID:K-1
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
lours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% 25% une—Aug. 25% Sept.—Nov. 25%
2016 �arch—May
16 �016 016
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po� Code Pollutants Method Code (Net afterFactor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2016
CO CO 0.08 08 0.000084
NOx NOx 0.09 08 0.0001
TSP TSP 0.01 08 0.0000076
PM10 PM10 0 08
PM2.5 PM2.5 0 08
S02 S02 0 08
VOC VOC 0.01 08 0.0000055
Control
HAP/TAP Emissions Emission Con
Pollutants (In Alphabetical CAS HAP/TAPS Estimation Efficiency EmissionEF Control
Order) (see instructions) (Pounds/Year) Method Code (Net after all Factor
See Instructions controls)
2016
Acetaldehyde 75-07-0 0.00003 08 1.52E-11
Acrolein 107-02-8 0.00003 08 1.8E-11
Ammonia as NH3 7664-41-7 5.9872 08 0.0000032
Arsenic Unlisted
Compounds(Specify ASC—Other 0.00037 08 2E-10
Component of ASC
Benzene 71-43-2 0.00393 08 2.1E-9
Beryllium Compound,
Unlisted(Specify BEC—Other 0.00002 08 1.2E-11
Component of BEC
Cadmium Metal(elemental
unreacted,Component of 7440-43-9 0.00206 08 1.1E-9
� } CDC
Chromium(VI) NSCR6—Other 0.00262 08 1.4E-9
Non—Specific,Unlisted
27

�V
(Specify Component of
NSCR6 CRC
- Cobalt Unlisted Compound
(Specify Component of COC—Other 0.00016 08 8.4E-11
COC
Formaldehyde 50-00-0 0.14033 08 7.5E-8
Hexane n— 110-54-3 3.3678 08 0.0000018
Lead Unlisted Compounds
(Specify and Component of PBC—Other 0.00094 08 5E-10
PBC
Manganese Unlisted
Compounds(Specify MNC—Other 0.00071 08 3.8E-10
Component of MNC
Mercury,vapor 7439-97-6 0.00049 08 2.6E-10
(Component of HGC
Naphthalene(Component of 91-20-3 0.00114 08 6.1E-10
POMT
Nickel metal(Component of 7440-02-0 0.00393 08 2.1E-9
NIC
Selenium Compounds SEC 0.00004 08 2.4E-11
Toluene 108-88-3 0.00636 08 3.4E-9
28

COPY of RECORD Date Submitted: 6/26/2017 17:01 :50
As entered in AERO
Facility Name: Triangle Brick Company—Merry Oaks Facility ID : 1900077
294 King Rd Permit: 06897
Moncure,NC 27559 County : Chatham
DAQ Region :RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
1. Emission Source ID(from permit)or K-1
Emission Source Group ID
2. Emission Source Description: Kiln 1—Natural gas/No.2 fuel oil/No. 6 fuel oil—fired brick tunnel kiln(14.5
tons per hour maximum brick production capacity,21.4 million Btu per hour
maximum heat input rate) [2D.1109 Case by C
3. Operating Scenario ED/Description: OS—2/Distillate fuel and NG combustion—secondary
4. SCC Number/Description: 305003 3 1/Brick Manufacture—Curing Firing; Curing and Firing: Dual Fuel
Fired Tunnel Kiln
Throughput/units in 2016:
,_.g.production or fuel use):
6. Fuel Information (if fuel is used) Sulfur % Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
tk-1 IVERTICAL STACKI 57.5 4 488 1 39.8 1 30008.49 ERP for Kiln 1
29

J
Operating Scenario: OS—2 Emission Source/Group ID:K-1
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
[ours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu)h ut:
an—Feb +Dec 25% 25% une—Aug. 25% �016
ept.—Nov. 25%
016 �arch—May
16 �016
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po� Code Pollutants Method Code (Net after Factor Ef Control
Pollutants (Tons/Year) (See Instructions) all controls)
2016
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP CAS Emissions Emission Control
Pollutants (In HAP/TAPS Estimation EfficiencyEmission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2016
F
30

COPY of RECORD Date Submitted: 6/26/2017 17:01 :50
As entered in AERO
Facility Name: Triangle Brick Company—Merry Oaks Facility ID : 1900077
294 King Rd Permit: 06897
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
1. Emission Source ID(from permit)or K-1
Emission Source Group ID
2. Emission Source Description: Kiln 1—Natural gas/No. 2 fuel oil/No. 6 fuel oil—fired brick tunnel kiln(14.5
tons per hour maximum brick production capacity,21.4 million Btu per hour
maximum heat input rate) [2D .1109 Case by C
3. Operating Scenario ID/Description: OS— 17/Residual Oil and NG combustion—tertiary
4. SCC Number/Description: 30500331/Brick Manufacture—Curing Firing; Curing and Firing: Dual Fuel
Fired Tunnel Kiln
Throughput/units in 2016:
,_.g.production or fuel use):
6. Fuel Information (If fuel is used) Sul f ur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point RP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
lk-1 IVERTICAL STACKI 57.5 4 1 488 39.8 1 30008.49 ERP for Kiln 1
31

Operating Scenario: OS— 17 Emission Source/Group ID:K-1
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
'[ours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 250�0 M 25"�u une—Aug. 25% Sept.—Nov. 25%
016 �arch— ay16 �016 016
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po�QS Code Pollutants Method Code (Net after Factor Ef Control
Pollutantss
(Tons/Year) (See Instructions) all controls)
2016
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
RAP/TAP AP CAS Emissions Estimation Control Emission
Pollutants (In (see instructions) HAP/TAPS Efficiency Factor EF Control
Method Code
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2016
32

V
40i0 NO
COPY of RECORD Date Submitted: 6/26/2017 17:01 :50
As entered in AERO
Facility Name: Triangle Brick Company—Merry Oaks Facility ID : 1900077
294 King Rd Permit: 06897
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
1. Emission Source ID(from permit)or K-2
Emission Source Group ID
2. Emission Source Description: Kiln 2—Natural gas/No.2 fuel oil/No. 6 fuel oil—fired brick tunnel kiln(14.5
tons per hour maximum brick production capacity,21.4 million Btu per hour
maximum heat input rate) [213.1109 Case by C
3. Operating Scenario ID/Description: OS—3/Natural gas combustion—primary
4. SCC Number/Description: 3050031 I/Brick Manufacture—Curing Firing; Curing and Firing: Gas—fired
Tunnel Kilns
Throughput/units in 2016: 0
,_.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry fines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
1K-2 VERTICAL STACK 57.5 4 488 39.8 30008.49 ERP for kiln 2
33

Operating Scenario: OS—3 Emission Source/Group ID:K-2
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
;[ours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% arch—May 25% une—Aug. 25% �016
ept.—Nov. 25%
2016 016 t016
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission Control
Pollutant Criteria Estimation EfficiencyEmission
o�QS Code Pollutants Method Code (Net afterFactor Ef Control
Pollutantss
(Tons/Year) (See Instructions) all controls)
2016
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
v0C v0C 08
HAP/TAP CAS Emissions Emission Control
Pollutants (in HAP/TAPS Estimation EfficiencyEmission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2016
34

COPY of RECORD Date Submitted: 6/26/2017 17:01 :50
As entered in AERO
Facility Name: Triangle Brick Company—Merry Oaks Facility ID : 1900077
294 King Rd Permit : 06897
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
1. Emission Source ID(from permit)or K-2
Emission Source Group ID
2. Emission Source Description: Kiln 2—Natural gas/No. 2 fuel oil/No. 6 fuel oil—fired brick tunnel kiln(14.5
tons per hour maximum brick production capacity,21.4 million Btu per hour
maximum heat input rate) [2D .1109 Case by C
3. Operating Scenario ED/Description: OS—4/Distillate fuel and NG combustion—secondary
4. SCC Number/Description: 30500331Brick Manufacture—Curing Firing;Curing and Firing: Dual Fuel
Fired Tunnel Kiln
Throughput/units in 2016: 0
,_.g.production or fuel use):
6. Fuel Information (if fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate Wfm)
Rectangle(L x W)
in 0.1 feet)
1K-2 IVERTICAL STACKI 57.5 1 4 1 488 39.8 30008.49 ERP for kiln 2
35

Operating Scenario: OS—4 Emission Source/Group ID:K-2
1�.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
fours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% arch—May 25% une—Aug. 25% �016
ept.—Nov. 25%
016 016 �016
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po�QS Code Pollutants Method Code (Net after Factor Ef Control
Pollutantss
(Tons/Year) (See Instructions) all controls)
2016
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP CAS Emissions Emission
Control
Pollutants (In HAP/TAPS Estimation Emission
(see instructions) Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2016
36

ve
p)o rjo-r 9/5j;&r E
COPY of RECORD Date Submitted: 6/26/2017 17:01 :50
As entered in AERO
Facility Name: Triangle Brick Company—Merry Oaks Facility ID : 1900077
294 King Rd Permit: 06897
Moncure,NC 27559 County : Chatham
DAQ Region :RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
1. Emission Source ID(from permit)or K-2
Emission Source Group ID
2. Emission Source Description: Kiln 2—Natural gas/No. 2 fuel oil/No. 6 fuel oil—fired brick tunnel kiln(14.5
tons per hour maximum brick production capacity,21.4 million Btu per hour
maximum heat input rate) [2D .1109 Case by C
3. Operating Scenario IIUDescription: OS— 18/Residual Oil and NG combustion—tertiary
4. SCC Number/Description: 3050033l/Brick Manufacture—Curing Firing; Curing and Firing: Dual Fuel
Fired Tunnel Kiln
Throughput/units in 2016: 0
,_.g.production or fuel use):
6. Fuel Information (If fuel is used) ro
Sulfur ,Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
(as listed inpermit)
9.Emission Release Point RP Information: Sources vented to more than one ERP use additional ntry tines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
1 K 2 IVERTICAL STACKI 57.5 4 488 39.8 30008.49 ERP for kiln 2
37

Operating Scenario: OS— 18 Emission Source/Group ID:K-2
__10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
`'[ours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% 016
25% une—Aug. 25% 016
25%
016 016 016 016
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency
Emission
(NAAQS) Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2016
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP Emissions Emission Control
Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2016
38

COPY of RECORD Date Submitted: 6/26/2017 17:01 :50
As entered in AERO
Facility Name: Triangle Brick Company-Merry Oaks Facility ID : 1900077
294 King Rd Permit : 06897
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory-Calendar Year 2016
1. Emission Source ID(from permit)or K-3
Emission Source Group ID
2. Emission Source Description: Kiln 3-Natural gas/No.2 fuel oil/No. 6 fuel oil-fired brick tunnel kiln(29 tons
per hour maximum brick production capacity,42.8 million Btu per hour
maximum heat input rate) [2D .1109 Case by Cas
3. Operating Scenario ID/Description: OS-5/NG combustion-primary
4. SCC Number/Description: 30500331Brick Manufacture-Curing Firing;Curing and Firing: Dual Fuel
Fired Tunnel Kiln
cz 5"O!3 rl— /%/ ram• err+
Throughput/units in 2016: 146235 TON/yr fjri' �r,oc ,c �a,•, o•� 20/3.
,...g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur ro
Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS-ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point RP Information: Sources vented to more than one ERP use additional ntry fines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
1 K-3 IVERTICAL STACK 75 1 5 1 450 51 60082.95 ERP for Kiln 3
39

Operating Scenario: OS—5 Emission Source/Group ED: K-3
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
[ours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 250�o 25"�o une—Aug. 25% �016
ept.—Nov. 250/o
016 �arch—May
16 016
13. Actual Emissions per Pollutant Listed:
Attach calculations and documentation of emission factors or other estimation methods used.
Emission
Emissions— Estimation Control
GHG CAS GHG Method Efficiency Emission Ef Control
Pollutants Pollutants Code (Net after Factor
(Tons/Year) (See all controls)
Instructions
2016
Emission
Criteria Emissions— Estimation Control
Pollutant Criteria Method Efficiency Emission
Po�QS Code Pollutants Code (Net after Factor Ef Control
Pollutantss
(Tons/Year) (See all controls)
Instructions
2016
CO CO 42.19 08 0.577
NOx NOx 9.21 08 0.126
TSP TSP J1 27.56 08 0.3769
PM10 PM10 * 27.56 08 0.3769
PM2.5 PM2.5 IP 27.56 08 0.3769
S02 S02 4.58 08 0.0627
VOC VOC 4.15 08
Emission
Emissions Estimation Control
HAP/TAP CAS Emission
HAP/TAPS Method Efficiency EF Control
Pollutants (In Alphabetical Order) (see instructions) (Pounds/Year) Code (Net after all Factor
(See controls)
Instructions
2016
Antimony Unlisted Compounds(Specify SBC—Other 9.32979 08 0.0000638
Component of SBC
Arsenic Unlisted Compounds(Specify ASC—Other 3.34878 08 0.0000229
Com onent of ASC
Benzene 71-43-2 424.0815 08 0.0029
Beryllium metal(unreacted) 7440-41-7 0.06142 08 4.2E 7
(Component of BEC
Cadmium Metal(elemental unreacted, 7440-43-9 0.84231 08 0.00000576
Component of CDC
Carbon disulfide 75-15-0 6.28811 08 0.000043
*':5,FE A rMc4<, ,o fir. / EEl 40

Chlorine 7782-50-5 190.1055 08 0.0013
Chromium Unlisted Compounds CRC-Other 3.05631 08 0.0000209
(Specify Component of CRC
Cobalt Unlisted Compound(Specify COC-Other 0.62442 08 0.00000427
Component of COC
Di 2-eth lhex 1 hthalate DEHP 117-81-7 292.47 08 0.002
Dibu 1 hthalate 84-74-2 20.4729 08 0.00014
Dichlorobenzene , 1,4- 106-46-7 7.01928 08 0.000048
Eth 1 benzene 100-41-4 6.43434 08 0.000044
Ethyl chloride chloroethane 75-00-3 83.35395 08 0.00057
Fluorides(sum of all fluoride
compounds 16984-48-8 67352.94 08
Formaldehyde 50-00-0 1,$ 08 d,moZlj
Hydrogen chloride(hydrochloric acid 7647-01-0 16679.01 08
Hydrogen fluoride(hydrofluoric acid as f'
mass of HF-Component of Fluorides
7664-39-3 27455.95 08
Lead Unlisted Compounds (Specify and PBC-Other 21.93525 08 0.00015
Component of PBC
Manganese Unlisted Compounds MNC-Other 12.37148 08 0.0000846
(Specify Component of MNC
Mercury,vapor(Component of HGC 7439-97-6 1.46235 08 0.00001
Methyl chloride 74-87-3 97.97745 08 0.00067
Methyl chloroform 71-55-6 0.6873 08 0.0000047
Methyl ethyl ketone 78-93-3 32.1717 08 0.00022
Methyl iodide 74-88-4 13.59986 08 0.000093
Methyl isobutyl ketone 108-10-1 12.42998 08 0.000085
Naphthalene(Component of POMTV 91-20-3 9.50527 08 0.000065
Nickel metal(Component of NIC 7440-02-0 1.87181 08 0.0000128
Perchloroeth lene tetrachloroeth lene 127-18-4 0.40946 08 0.0000028
Phenol 108-95-2 12.57621 08 0.000086
Selenium Compounds SEC 6.25886 08 0.0000428
Styrene 100-42-5 2.9247 08 0.00002
Toluene 108-88-3 23.3976 08 0.00016
X lene 1330-20-7 9.79775 08 0.000067
X lene,o- 95-47-6 8.48163 08 0.000058
'��'�t`.�fyr�! `x.�°�h��1� �.vb.' .�► 2�t� � ��� r�..����isi-► ..� 20<�.
41

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COPY of RECORD Date Submitted: 6/26/2017 17:01 :50
As entered in AERO
Facility Name: Triangle Brick Company—Merry Oaks Facility ID : 1900077
294 King Rd Permit : 06897
Moncure,NC 27559 County : Chatham
DAQ Region :RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
1. Emission Source ID(from permit)or K-3
Emission Source Group ID
2. Emission Source Description: Kiln 3—Natural gas/No. 2 fuel oil/No. 6 fuel oil—fired brick tunnel kiln(29 tons
per hour maximum brick production capacity,42.8 million Btu per hour
maximum heat input rate) [2D .1109 Case by Cas
3. Operating Scenario ID/Description: OS—6/Distillate and Natural gas combustion—secondary
4. SCC Number/Description: 30500312/Brick Manufacture—Curing Firing;Curing and Firing: Oil—fired
Tunnel Kilns
Throughput/units in 2016:
1-g.production or fuel use):
6. Fuel Information (If fuel is used) ro
Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
�__l I i
9.Emission Release Point RP Information: Sources vented to more than one ERP use additional ntry fines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
1K-3 VERTICAL STACK 75 5 450 51 60082.95 ERP for Kiln 3
42

Operating Scenario: OS—6 Emission Source/Group ID:K-3
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
[ours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 250�o M 25% une—Aug. 25"�u Sept.—Nov. 25%
2016 �arch— ay
16 �016 1
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po�QS Code Pollutants Method Code (Net after Factor Ef Control
Pollutantss
(Tons/Year) (See Instructions) all controls)
2016
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP CAS Emissions Emission Control
Pollutants (in HAP/TAPS Estimation EfficiencyEmission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2016
43

Ve
1�id AO—r OOPE0r'& Vc/17;4 O,,L-
COPY of RECORD Date Submitted: 6/26/2017 17:01 :50
As entered in AERO
Facility Name: Triangle Brick Company—Merry Oaks Facility ID : 1900077
294 King Rd Permit: 06897
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
1. Emission Source ID(from permit)or K-3
Emission Source Group ID
2. Emission Source Description: Kiln 3—Natural gas/No.2 fuel oil/No. 6 fuel oil—fired brick tunnel kiln(29 tons
per hour maximum brick production capacity,42.8 million Btu per hour
maximum heat input rate) [2D.1109 Case by Cas
3. Operating Scenario ID/Description: OS— 19/Residual Oil and NG combustion—tertiary
4. SCC Number/Description: 30500331/Brick Manufacture—Curing Firing; Curing and Firing: Dual Fuel
Fired Tunnel Kiln
Throughput/units in 2016:
,_.g.production or fuel use):
6. Fuel Information (If fuel is used) /a Sul fur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
�__l i - i
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
1K-3 IVERTICAL STACK 75 1 5 1 450 51 60082.95 ERP for Kiln 3
44

Operating Scenario: OS— 19 Emission Source/Group ID:K-3
_l0.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
'[ours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% arch—May 25% une—Aug. 25% �016
ept.—Nov. 25%
016 016 �016
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG . Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po� Code Pollutants Method Code (Net after Factor Ef Control
Pollutants (Tons/Year) (See Instructions) all controls)
2016
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP CAS Emissions Emission Control
Pollutants (in HAP/TAPS Estimation Efficiency Emission EF Control
Alphabetical Order) (Pounds/Year) (Net after all controls)
(see instructions) Method Code y Factor
See Instructions
2016
i
45

COPY of RECORD Date Submitted: 6/26/2017 17:01 :50
As entered in AERO
Facility Name: Triangle Brick Company—Merry Oaks Facility ID : 1900077
294 King Rd Permit: 06897
Moncure,NC 27559 County : Chatham
DAQ Region :RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
1. Emission Source ID(from permit)or SD-1
Emission Source Group ID
2. Emission Source Description: Natural gas—fired rotary coatings dryer(0.3 million Btu per hour maximum
heat input) [NSPS UUU]
3. Operating Scenario ID/Description: OS—20/Natural Gas Combustion
4. SCC Number/Description: 30500301/Brick Manufacture—Dryer;Raw Material Drying
5. Throughput/units in 2016: 720 TON/yr
(e.g.production or fuel use):
Fuel Information (if fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
FUGITIVE(NO ERP for Fugitive
EP—FUG STACK 1 7? Area= 1 source
46

Operating Scenario: OS —20 Emission Source/Group ID: SD-1
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
[ours per Day ( 4 ) Days per Week ( 3 ) Weeks per Year ( 10 )
11.Typical Start& End Times For Operating Scenario: Start: 800 End: 1200
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 0% arch—May 50% une—Aug. 50% �016
ept.—Nov. 0%
016 016 �016
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission
Pollutants
Code Pollutants Method Code (Net after Factor Ef Control
(Tons/Year) (See Instructions) all controls)
2016
CO CO 6' .pile, 09 d.Uf
NOx NOx 0,v 1 09 o,C>Z7'
TSP TSP 0.01 08 0.02
PM10 PM10 0.01 08 0.02
PM2.5 PM2.5 0.01 08 0.02
S02 S02 08
VOC VOC 08
Emission Control
HAP/TAP CAS Emissions Estimation Efficient Emission
Pollutants (in HAP/TAPS y EF Control
Alphabetical Order)
(see instructions) (Pounds/Year) Method Code (Net after all Factor
See Instructions controls)
2016
Formaldehyde 50-00-0 09 4.ico
O.Qp�
47

Facility Total CY 2016 Emissions Summary
COPY of RECORD Date Submitted: 6/26/2017 17:01 :50
As entered in AERO
Facility Name: Triangle Brick Company-Merry Oaks Facility ED : 1900077
294 King Rd Permit : 06897
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory-Calendar Year 2016
Record Facility-Wide Totals From all Permitted and Non-Permitted Air Pollutant Emission Sources
Green House Gases Pollutants(GHG)
Actual Emissions Tons/Year
Pollutant CAS 2016 2015 % Change
Criteria Pollutants
Actual Emissions Tons/Year
Pollutant CAS 2016 2015 %Change
CO CO 42.27 40.57 4.1902905%
NOx NOx 9.3 9.07 2.535838%
PM TSP TSP 35.67 34.2 4.298238%
PM10 PM10 33.47 25.35 32.03156%
PM2.5 PM2.5 33.47 25.35 32.03156%
S02 S02 4.58 4.85 -5.56701
VOC VOC 4.75 5.28522 -10.126733%
Hazardous Air Pollutants S and/or Toxic Air Pollutants APs
Actual Emissions Pounds/Year
Pollutant I CAS 1 2016 1 2015 % Change
Pollutant Group:Antimony Compounds total mass inc elemental SB Group Sum:9.32979
Antimony Metal-add to SBC 7440-36-0 1 0.0 .06743 -100.0%
Antimony Unlisted Compounds(Specify SBC-Other 9.32979 8.87847 5.0833044%
Com onent of SBC
Pollutant Group:Arsenic Compounds(total mass of elemental AS,arsine and all inorganic compounds) Group
Sum:3.34915
Arsenic Metal,elemental unreacted 7440-38-2 0.0 .03181 -100.0%
(Component of ASC
Arsenic Unlisted Compounds(Specify ASC-Other 3.34915 3.18714 5.0832396%
Component of ASC
Pollutant Group:Beryllium compounds Total mass Group Sum:.06144
Beryllium Compound,Unlisted(Specify BEC-Other 2.0E-5 .00002 0.0%
Component of BEC
Beryllium metal(unreacted)(Component 7440-41-7 0.06142 .06441 -4.642136%
of BEC
48

Pollutant Grou :Cadmium compounds total mass inc elemental metal Group Sum:.84437
Cadmium Metal(elemental unreacted, 7440-43-9 0.84437 .82948 1.7951024%
Component of CDC
"Autant Grou :Chromium VI Non-S ecific Compounds,as Chrom (Component CRC Group Sum:.00262
Chromium(VI)Non-Specific,Unlisted NSCR6-Other 0.00262 .033 -92.0606%
(Specify Component of NSCR6 CRC
ollutant Grou :Chromium-All/Total Inc Chromium cate ories,metal and Others Group Sum:3.05893
Chromium(VI)Non-Specific,Unlisted NSCR6-Other 0.00262 .033 -92.0606%
(Specify Component of NSCR6 CRC
Chromium Unlisted Compounds(Specify CRC-Other 3.05631 3.03472 0.7114329%
Component of CRC
Pollutant Grou :Cobalt compounds
Grou Sum:.62458
Cobalt Unlisted Compound(Specify COC-Other 0.62458 .59888 4.2913494%
Component of COC
Pollutant Grou :Lead and Lead compounds Group Sum:21.93619
Lead Unlisted Compounds(Specify and
Component ofPBC PBC-Other 21.93619 21.04961 4.2118573%
Pollutant Grou :Man anese compounds roup Sum:12.37219
Manganese Unlisted Compounds(Specify MNC-Other 12.37219 11.8884 4.0694323%
Component of MNC
Pollutant Group:Mercury Compounds-all total mass,inc Hg Vapor Group Sum:1.46284
Mercury,vapor(Component of HGC 7439-97-6 1 1.46284 1 1.40806 T 3.8964598%
Pollutant Grou :Nickel Compounds,sum total mass,inc elemental Group Sum:1.87574
Nickel metal(Component of NIC 7440-02-0 1.87574 2.10671 -10.963536%
ollutant Grou :Pol c clic Organic Matter(Specific Com ounds from OA PS for TV Group Sum:9.50641
`'Na hthalene(Component of POMTV 91-20-3 9.50641 9.11523 4.2914996%
Acetaldehyde 75-07-0 3.0E-5 .00003 0.0%
Acrolein 107-02-8 3.0E-5 .00003 0.0%
Ammonia as NH3 7664-41-7 5.9872 5.5488 7.900804%
Benzene 71-43-2 424.08542 406.63545 4.291309%
Carbon disulfide 75-15-0 6.28811 6.02937 4.2913265%
Chlorine 7782-50-5 190.1055 182.28322 4.291279%
Di 2-eth lhex 1 hthalate DEHP 117-81-7 292.47 280.43573 4.291276%
Dibu 1 hthalate 84-74-2 20.4729 19.6305 4.2912793%
Dichlorobenzene , 1,4- 106-46-7 7.01928 6.73046 4.291234%
Eth 1 benzene 100-41-4 6.43434 6.16958 4.2913785%
Ethyl chloride chloroethane 75-00-3 83.35395 79.92418 4.291281%
Fluorides sum of all fluoride compounds) 16984-48-8 67352.94 62817.60299 7.219849%
Formaldehyde 50-00-0 18.73034 37.90666 -50.58826%
Hexane n- 110-54-3 3.3678 3.1212 7.9008045%
Hydrogen chloride(hydrochloric acid 7647-01-0 16679.01 35584.66685 -53.128666%
Hydrogen fluoride(hydrofluoric acid as 7664-39-3 27455.95 58273.92187 -52.88467%
mass of HF-Component of Fluorides
Methyl chloride 74-87-3 97.97745 93.94597 4.291274%
Methyl chloroform 71-55-6 0.6873 .65903 4.2896385%
Methyl ethyl ketone 78-93-3 32.1717 30.84793 4.291272%
Methyl iodide 74-88-4 13.59986 13.04026 4.2913246%
Methyl isobutyl ketone 108-10-1 12.42998 11.91852 1 4.2913070/(
Perchloroeth lene tetrachloroeth lene 127-18-4 0.40946 .39261 4.2917895%
49

Phenol 108-95-2 12.57621 12.05874 4.2912474%
Polycyclic Organic Matter(Inc PAH,
,I;oxins,etc.NC AP 42 historic amorphous POM 0.0 .04239 —99.99999%
lob
Selenium Compounds SEC 6.2589 6.00136 4.2913647%
Styrene 100-42-5 2.9247 2.80436 4.291179%
Toluene 108-88-3 23.40396 22.44076 4.292188%
X lene 1330-20-7 9.79775 9.4559 3.615206%
X lene o— 1 95-47-6 8.48163 8.07134 5.083304%
50

COPY of RECORD Date Submitted: 6/26/2017 17:01 :50
As entered in AERO
Facility Name: Triangle Brick Company—Merry Oaks Facility ID : 1900077
294 King Rd Permit: 06897
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
Comments From Facility:
6/26/2017 —General Comments
General Comments : The HF,HCl and total fluorides emissions reflect the operation of the DLA for the last 4 months of the
year.
51

_ t
SUPPORTING EMISSION CALCULATIONS
TRIANGLE BRICK COMPANY-MERRY OAKS

Table A-1
Calculation o1 Actual 2016 Air Emissions From Brick Tunnel Kiln%1
(Source I.D.-K-1)
Triangle Brick Company
Merry Oaks,North Carolina
Production Data
Tonsal Fred-Pre,u 0tom
Cudc Fe NNural Ges ComMstetl 1a" tt'
Gelbm D.IW.Oil Gomb_ D albm
GalWns R-I.i Oil DOmM#W alWna
Tons Bndr Feed Wib Nelurel Gas 0 tore
Tons Bank Find WMh DiWIWU Oil 0 tom
Tom 9rick FrM WMh Residua101 0 1om
Prima O fi BcemM Semrga n Stern. T.- 0-fine 0-fine S rerio Emisaone Summa
NC TAP Or Fin Ne 1Gas Cla Fin Di,bi O' Distlllete Fuel ComMWion' Tob1 CW Fin Resdual Oii Residual Fwi TOM
i..
Polluhnr CAS Num4r HAP Emistion Adel Emisswn ActualEmrssian Actual r.S n. E.-m -1 Emission Tare1.1. -1.1.
factor EmbNon Rab Facto Emisswn Rita Fad Emr n Rate Emissiom Factor Ern ron Rate Fador b Emi Emuswm Mnon t` N1000 arlbn rebel Ibs1 I_. Ib.V r w- Ilon Ds ns TSP' N.- 0.13 000 0,13 0'W 2.0 ow 000 0.13 cw 225 0.0D 0.W
PM-10' Neither 0.13 ow 0,13 ow 1.1 p00 0.00 0.13 0.00 19.6 O00 ow
PM-2.5' NeitMr 0.13 ow 0.13 0.00 1.1 0.00 0.00 0.13 0.00 isms 0.00 0.00
NaNMr 0.0127 O.oO color 0.00 710 0.00 ow c082] O.110 329.7 O.l1D 0.00
NeitMr 0.126 O.oO 0.128 0.00 20.0 0.00 am 0.128 ow We am 0.00
NeitMr 0.57] poll 0.577 O.oO 50 0.00 0.00 p577 am 5.0 0.00 0.00
NeitMr OO568 O.oO 0.0588 Moo M2 ow cm O.. 0.00 0.3 0.00 00071-556 TAP/HAP 4)O 0.00 4.70E-09 ... WA 0.00 0.00 4.70E-09 ow WA 0.00 0.00
1,a DicNoroMrMane 10s4 7 TAP/HAP 480E-05 O.oO 4s0E-05 000 WA 0.00 000 4.80E-05 0.00 WA 0.00 0.00 0.00 0.00
2-BuA re WEEK? 78936 TAP/MAP 2.20E-04 c00 2.20E01 0.00 WA 000 0.00 2.20E-04 nor, WA 0.00 0.00 0.00 0.00
2.Hasemna MI9 WI-7s6 TAP/HAP 8.50E-05 &W 850E-05 0.00 N/A 0.00 000 8.50E-05 000 WA 0.00 000 000 000
Acetone 67�1 Nelmer t70E4 ow 1.7 s(M 0.00 NIA 000 0.. 1.70E4 0.00 WA ow O.oO coi &W
AMimo Sa000rer HAP 8.38E-05 coo 838E-0S 0.00 WA 0.00 0.00 8.39E-05 0.00 5.75E-03 ODD ow 0.00 04M
Arwnic ASCgtrr TAP/HAP 229E-05 cm 2.2 46 ODO 5.92E-04 0.00 O.OD 2.29E-05 0.00 1.32E-03 0.01D ow o.w 0.00
%_ 71J 2 TAP/HAP 290E-0D 0.00 290E-03 0.00 WA 0.00 0.00 290E-03 0.00 2.1.- o. Opp 0.00 ow
M Ilium - TAP/HAP 420E-07 0.00 420E-07 ow 3.53 0.00 0.00 4.20E-07 D00 2.78E-05 0.00 pop cm 0.00
Ns -e IM. PNMWre 117-81-7 HAP 2.00E-03 0.0D 2.0M42 am WA 0.00 0.00 2.OUE-03 0.00 WA ow ow 0.00 cw
M thalate -7 NeitMr 180E-05 0.00 1.80E-05 0.0D NIA 000 0.00 1.80E-0s 0.00 WA 0.00 ow ow cW
Cadmium 7440435 1 TAPIHAP 1 5.7s 000 378E-05 I 000 1.55E-03 0.W 0.00 5.78E-09 0.00 3.98E-0I 0.00 MOD 0.00 0.00
Grbon DiauMide Mist, TAP/HAP 430E-05 1 0.00 4.30E-05 0.00 WA 000 0.00 4.30E-0S 0.00 WA O.oO 1 0.00 1O.OD 0.00
CNlonm 7782-506 TAP/MAP 130E-03 ow1.30E- 0.00 WA 0.00 000 1.30E-03 O.OD WA 000 0.00 0.00 0.00
CM1loroetMm 75-003 HAP 5.70E- 0.00 5.70E-0I O.Oo WA 0.00 0.00 5.70E-0I 1 0.00 1 WA I 000 I OOD I0.00 0.00
Chlom.0e 7"7-3 HAP 8.70E-04 0.00 8.70E-0I Doe WA 0.00 0.00 870EM 1 0.00 NIA D.00 I am IO.oO 000
Ch,o;7 VI4 NSCR6 r TAPIHAP WA 0.00 N/A coo 2.38E-03 ow 0.00 NIA 1 000 1 2.48E-04 0.00 1 coo I000 0.00
Chromium CRCOIMr HAP 2.09E-05 I poll 2.09E-05 O.w 8.11E-03 0.00 000 2.09E-05 I 0.00 I s.45E-04 1 0.00 1 00o IO.oO 000

Table A-i
Calculation of Actual 2016 Air Emissions From Brick Tunnel Kiln/1
(Source I.D.-K-1)
Triangle Brick Company
Merry Oaks,North Carolina
Production Oala
Tons of Flretl&id Protlucvd 0 tom
Cu-Feat Natural Gas Comausletl 1571
Gelbns Disblbte Oil Comb- 0 elbm
G,li-R-.1 Oil Combustetl p albm
Ton.Grid Firotl Wn,Nduml Gas 0 tom
Tons BRd Flratl WN Die"o Oil 0 hm
Tons BRd Firatl Wtb Ro-I Oil 1 0 tom
p,ma Oco.in,Swnarb SBwMa ratio Sce Tama O S-- Emi ns Summa
NCTAP 8111 Cle Fdn Nffiural Gaa Cla Fin Diffiillde Oi Doufllala Fwl Combustion" Toh1 Cla Fin ResiEual Oil Rasbual Fwl Comtwatlori Total ss
PoBubrB CAS Number HAP Emisson ActwI Emiasiw Adw1 Em".n Aqua) O r_Swn. Err- - Emisaion Actual ow,Sce,. Tota120Is Toh1.18
Factor Err-Rah Fa-r Emission Rata F.- Emhoio,Rate Emissiom Factor Emission Rate Fa- Emi-Rose Emisabns Emissions Emwbm
bslon Ihalon I Idt000 Ibn bsdon Ibsr d100p elbn I I Ibs
Cgbtt COCOINer HAP 1.27E-08 000 462>E-0B ow NIA 000 0.1X/ 427E-08 am a02E-03 0.00 0.00 0.00 0.00
DI IPM1Melab 84-74.2 HAP 1 IDE-04 0.00 1640E-0a DOW NIA 0.00 0.00 1.40E-04 ow WA ow 0.00 DOW am
Ue hb 8458-2 Na , 2,10E-04 0M 2.40E-04 ow NIA 0-00 am 240E-04 0.00 WA 0.00 0.00 0.00 0-00
EI Bemam 10041.1 HAP 440E-05 0.00 4.40E-05 0.00 WA Mw 0.00 4.0E-05 DM 838E-05 am 0.00 0.00 am
Formekb M' -coc TAPIHAP WA 0.00 WA ow 4.80E-02 ow DOW WA0.00 4.25E-02 DOD 0.00 Doc 0.00
N d en CNbriM ]8-o TAPIHAP 1 7DE-01 0.00 1.70E-01 0.00 NIA am 0.00 120E-01 0.00 NIA 0.00 O.OD 0.00 0.00
H tl an Flwritle 7864.393 TAPIHAP 280E-01 0.00 2.80E01 0.00 WA 0-00 ow 2.80E-01 0.00 WA 0. 0.00 080
IodomaMem 7458-4 HAP 930E-05 O.OD 9.30E-05 am WA 0.00 0Do 9.30E-05 0.00 WA 0.00 0.00 0.00 owLee PBCQm! HAP 150Ed ow1.50E-04 OM125E-03 000 ow1.50E-04 0.00V.E� .W
+13 SOD ow ..Do 0.00
Ma 14s1COYiar TAPIHAP 846E-05 0.00 8.48E-05 0.00 1.97E-03 0.00 0-0O 8.46E-05 0.00 -03 0.00 am 000 ow
Merw a ]aA3TE TAPIHAP 1.00E-05 O.OD 1.00E-05 0.00 4.23E-04 0.00 0.00 1.00E-05 0.00 -04 ow 000 0.00 am
Ne Ibelem 91-20-3 HAP 850E-05 0.00 6.50E-05 0.00 WA 000 0.00 8.50E-05 am -0J 000 000 0M DOD
Ni-' 74 1. TAPIHAP 128E-05 0.00 1.28E-05 0.00 240E-12 0.00 aw 128E-05 0.00 -02 one 000 0.00 0-0O
PMrwl 10&9S2 TAPIHAP 8.80E-05 0.0D 8.80E-05 0.00 WA 0.00 am 860E-05 0.00A 0.00 000 0.00 0.00
Po clic nic Matbr pcsi TAP NIA MOD NIA 0.00 3.30E-0J Do) ow NIA 0.00d3 am 000 O.OD Mw
Sabnium SEC HAP 4.28E-05 0OD 4.28E-05 0.00 WA 0.00 ow 4.28E-05 0.00 -01 0.00 000 0.00 0.00
100425 TAPIHAP 200E-0S 0.00 2.00E-05 0.0p WA 0.00 am 2.00E-05 OAOA 0.00 am ow 0.0o
TNraMloro - 127-18.4 TAPIHAP 2.80E-08 a00 2.80E-0B 0.00 WA 0.00 ow 2.80E-M 0.0DA ow 0.00 0.00 000
Tolwm 108.8&3 TAPIHAP 180E-04 0-00 1.80E! 0.00 WA 0.00 0.00 1.60E-04 0.00 -03 0.00 ow 0.00 0.00
Total Fluo,tlm 1mB4.N5 TAP 148E-01 0.00 4.48E.1 0.00 WA O.00 0.00 4.18E-01 0.00A p.00 O.00EMO 0.00 000
Xybna 1336207 TAPIHAP 1.25E-01 0.00 1.25E-0a D.00 WA 0.00 0.00 1.25E-01 D.ODM OAO 0.00 O.00 000
EmissloI%do'baaatl w pSEPI Sdd A-doI,d of NCM G, M-l0 000 ed warts P d-AEfk ffi Trbrple Brick ComwMa Merry Oaks.NOR,Carolim facility.
ta.Emsffian latler for TSP based on Sbd Ten dahtl Aupuffi 200fi.PM-10 effi wuel to TSP due h AERO IIm9laon.
2. Emission factors aMaimtl Irom AR42 Sagion 113'Bnd antl StructuMl Cby Protluc[s',Fiml report,Aupuffi 18B].
3. Umorarolbtl emissbn(agar for Hytlropan FIuo�Ma based on warp last wmplatetl Odcbar 1895.
4. Fwlwmbuffiion em'rssion hgors obtaimdIrom AP-42 SeGon 1.3'Fual Oil Combugion'ard NCDEM 9Wtlawa.
5. Heat inWt rotilp assumM to be 140,OW BW9albn for No.2lwl oil entl 150.000 BtWpal for No.B fwl dl.
6. Sulfur wMem of No.2 fuel oil essumatl to be O5%.
>. 5ullurwnhm o!No6 oBaw le(1to
8. Emission lector for Tooll rid Flwal (1.8)x(Hydro9ln FlwRdl lmbffion Iago).
from APi2
om W TAP
m CAA HAP
rom AERO

Table A-2
Calculation of Actual 2016 Air Emissions From Brick Tunnel Kiln Y2
(Source I.D.-K-2)
Triangle Brick Company
Merry Oaks,North Carolina
Pro6uNon D-
Ton,of Fi and,Pro0uce0
C,Wc F.N Natural Gaa Combusle4 tns
G..R.Dist"_Oil Combu.teE Ibm
Ga Resi IOil 1`
ambuWe4 Ions
Tom Baal F.-With Natural Gas 0 Wn.
Tem BI.Free WM Dstillete Oil 0 tone
Ton.&idh Feb WM Ree 1 Oil 0 tom
Pnaw 0 b SC.m110RE..
SamMa ret Sc Red. Terra O tin Scemrb Emi,s Somme
NCTAPaR, Cl,,fin Nat Ga. n at Gea DIusu.F.1 Combusll.n' T.fel Cla Fir Nat Ga, ReaWual FUN Combwtbn' T.
PoIIN.M CAS NumWr HAP Emkuon -1 Ac Em Actual o­Sean, Emission Adual Emi..Wn -1 O r.Sc.n. Tote12016 T..'2ma
Fargo Emmhon RateEm wn R.I. Fedor Emh an Rate Emissrom Fedor Emh hon Rat. Factor Emi n Rate Emissrons Emi Em2Non.
beAan bsl bsl lbsAon .- IdiOW Ibn 1 b,l Ibs race WnsTSP' N.4- 013 0.00 000 20 000 000 0.13 0.00 22.5 0.00 0.to 000 0.00PM-10' N. r 013 000 0.00 1.t 0.00 0.00 0.13 0.00 198 0.00 0.00 000 OAOPM-2.5 Neither 0.13 0.00 0.00 1.1 0.00 0.00 0.13 000 tab 0.00 0.00 0.00 0.00
SooNa r 00027 000 0.00 71.0 0.00 am 0.0w 0.00 3n,7 0.00 0.00 000 0.00
Nwffor 0.126 ow 0.00 20.0 0.00 0.00 0.126 000 .0 0.00 000 000 0.00
Ne OSrr am 000 5.0 0.00 0.00 0.577 0.00 50 0.00 am 000 0.00
N. ODGes o. 0.00 0.2 0.00 0.00 0.0566 0.00 0.3 0.00 o. o. a.
1 11 Trkhbmelmm' 1�­,R
TAP/HAP 4.70E-06 0.00 4.70E-06 090 WA 0.00 G.00 4.7OE4b OAO NIA 0.00 0.00E+00 ow 0.w
1 A dMIom . 7 TAPIHAP 4.80E-05 0.00 4.80E-05 0.00 WA MOD 0.00 4.80E-05 0.00 NIA 0.00 000E+0D ow 0.00
2-aulanom MEK TAPIHAP 2.20E-01 G.00 220E-01 0.00 WA ow 0.00 2.20E-04 0.00 WA 0.00 0.00E+00 0.00 ow
2-Hexamne MIB TAPIHAP 850EA5 000 a50E-05 ow WA 0.00 0.00 850E-05 0.00 WA am 000E+00 ow Opp
Acetone Neither 1.70E-03 ow 1.70E-03 ow WA 0.00 0.00 170E-03 0.00 WA 0.00 0.00E+00 0.00 0.00
AMimon r HAP 6.36E-05 0.00 6.38E-05 0.00 N/A o. 0.00 638E-05 0.00 525E-03 0.00 000E+00 0.00 0.00
Arum. r TAP/HAP 229E-05 ow 2.28E-05 0.00 592E-0a 000 0.00 2.28E-05 0.00 1.32E-03 0.00 0.00E+00 0.00 0.00
a.rizene TAPIHAP 290E-03 0.00 2.90E-03 0.00 N/A 000 0.00 280E-03 0.00 2.14E-01 ow 000E+00 0.00 0.00
ae Ilium TAPIHAP 420E-07 0.00 4.20E-07 000 3.53EM 000 o0D 420E 0.00 278E-06 000 0.00E+00 0.00 0.00
Lz -et IMx PMha 7 HAP 2.00E-03 OAD 200E-03 000 WA 0.00 0W 2AOE-03 0.00 WA 0.00 000E+00 0.00 0.00
9 IM MW Neither 1.80E-05 0.00 180E-05 0.00 WA 0.00 0.00 180E-05 0.00 WA 0.00 000E+00 000 0.00
GEmium -5 TAPIHAP 5.78E-06 0.00 5.'r8E48 0.00 1.55E-03 0.00 0.00 5.76E-06 0.00 3.99EM 0.00 0.00E+00 0.00 0.00
Carbon N, 75.150 TAPIHAP 4.30E411 0.00 130E-05 0.00 NIA 0.00 0DO 400E46 0.00 WA 0.00 000E+00 0.00 0.00
Chlanm 7rez-50.5 TAPIHAP 1.00E-03 0.00 1.30EZ 0.00 WA 0.00 0.w 1.30E-03 0.00 WA 0.00 0.00E+00 0.00 0.00
ChbmatheM 75 HAP 5.70EO0 0.00 5.7t 0.00 WA oww 1 0.00 1 5.70EM ooD WA 0.00 1 0.00E+00 I 0.00 0.00
CHlomm.tham 7-7.3 HAP I 6.70E-00 1 0.00 870E-0n OWO I WA f 0.00 1 0.00 1 6.70EM o0D WA 0.00 1 000E+00 1 0.00 000
Chrome vl' NSCR TAPIHAP I NIA 0.00 N. 0.00 236E-03 o(G oW NIA o. 2.18E-01 0.00 0.00E+00 0.00 0.00
Chromium CRCO , HAP 2.08E-05 0.00 2.119E-05 0.00 6.11E-03 0.00 0.00 2.09E-03 0.00 B.d5E41/ 0.00 0.00E+00 000 0.00

Table A-2
Calculation of Actual 2016 Air Emissions From Brick Tunnel Kiln e2
(Source I.D.-K-2)
Triangle Brick Company
Merry Oaks,North Carolina
Pmductlon Dsh
Tons of Fretl Wn Pmdwetl tans
Cudc Feet N-W GS Gmdnted Ns
Gslbns Distilbte Oil Combu9ed albns
Galbna R.-Oil Gmbwhd albns
Tons Brick Fi-WM N.-Gas 0 hna
Torn.M&Fire Wth Distilhh Oil 0fora
Ton Bndk Fired Wth R,s$OII 0 bfb
Rirw O b8 s-no S- Scenana Tenia 0 rao Swnarb Emissions Sumno
NCTAP6lar Cla Fin Nat Gas Cle FWn Nat.Gas Distilhte Fuel Combustion' ToblM---
Fin Nat,Gas RaeWual Fuel Gmbustbn- Tool
PoNWrR CAS Numbr HAP Emissbn Actual Emission Astwi Emission Actual .Scan. on Actual EmW n Actwl r.Scan. Tob1"IS Toh12016
Factor Emission Rate F.- Emission Rare Factor Emiuun Rah Emissonsr Emisson Rate Factor Emission Rah En i- Emb Emiwion
Ibanon Ile IbNton Id1000 albs lednCob ft COCOIIwr HAP 4.27E-06 0.00 427E-06 0.W NIA 0.W 0.008 000 6.02E-03 0.w 0.00E+00 0.00 0w
g IPhlulab 84]42 HAP 1.a0E-0< 0.to 1AOE-01 04W NIA 0.00 0.004 cW WA 0.00 O.00E+W OA0 0.00
Di hb 84-08-2 Ns6Mr 2.40E-0i aw 2.40E-01 O.w WA 0-00 0.w -01 ow WA 0.00 0.00E+00 0.00 0.00
E r¢e10641J HAP 4AOE-05 0.00 4.40E-05 0.W NIA ow OAO -05 0.00 8.98E-05 O.DD 000E+00 0.00 0.00
F, Web de 50 TAP/HAP WA 0.00 WA 0.00 4aDEO2 0.00 0.00 0.00 4.25E-02 0.00 O.00E+W 0.00 0.00
en Cllbrke 164]-01-0 TAP/HAP 1.]OE-01 000 1.]OE-01 cm NIA 0.W 0.00 -01 cw WA 000 000E+00 0,00 0.00
Xd en Flwritle T66139J TA-P 260E41 0.00 2.60E-01 0.00 WA M. 0.00 -01 o. WA 0.OD 0.00E+00 ow MOD
lodomemane- ]441&4 HAP 930E-05 0-00 9.30E-05 0-00 WA 0.00 0505 ... WA 0.00 O.WE+W 0.00 0.00
leaf P8OOw's, HAP 1.50E-04 000 1.50E-04 O.W 1.25E-09 0.00 0.00 150E-04 oW 1.51E-03 oW 000E+00 oM 0.00
Man anew' Mric h TAP/HAP 8.48E-05 0.00 6.48E-05 0.00 1.91E-03 0.00 0.00 846E-0S 050 300E-03 O50 000E+W 0.00 0.00
Mercu 74399 TAP/HAP 100E-05 ow 100E-05 0.00 4.23E-04 0.00 0.00 1.00E-05 ow 1.13E-04 OAO 000E+00 0.00 050
91-20J HAP 6-E46 ODD 8.50E-05 0.W NIA 0.00 ow 6.50E45 0.00 1./9EO3 0M 0.00E+00 0to 0.00
rva Niticel ne 7440-020 TAPIHAP 1.28E-05 ow 1.26E-05 0w 240E-02 a 0w 128E-05 0w a45E-0Q 0.to 000E+. ow 0.00
Phenol IW952 TAP/MP a60E-05 ow 8..E-05 0.00 WA 0.00 0.00 SWE-06 0.00 WA 0.0) 0.00E+00 ow OAO
Po cgc sic Meaer Post TAP WA too WA 0.00 3.WE- 0.00 0.00 WA 0.00 12 .03 0.00 000E+00 ow 000
Sahnlum SEC HAP 428E-06 0.to 4.28E-05 0.W WA ow 0.00 1.28E-05 0.00 889E-04 O.OD 000E+00 0.00 O.
S a 100425 TAPIHAP 200E-05 OW 2.00E-05 cW WA O50 050 200E-0S OAO WA OM 050E+00 0.00 0.00
T�traWoroelNaw 127-184 TAPHAP 280E-08 0.D0 280E-08 0.00 WA 0.00 ow 280E-08 ow WA O.W 0.00E+W 000 000
Tolww 108-6&9 TAP/HAP 1 BOE-0/ 0.00 1.80E-01 O.OD NIA 0.00 0.00 1.60EM 0.00 8.20E-03 0.00 0.00E+00 0.00 0.00
Tahl FluoMea 1aeBId68 TAP 448E-01 ow 4.48E-01 0.00 WA 0.00 050 4.46E-01 0.00 WA 0. 0.00E+00 -WW 0.00
%Yhw 1330-20] TAP/HAP 125E-04 0.00 1.25EO1 0.00 WA 0.00 0.00 1.25E-0I D.00 1.09E-01 0.00 0.00E+00 0.00 0.00
1. Ertneelor f-r Dasetl on USEPr S Aswci,W of uwt t06 -10 wt d source fast w AER at Trbigle Back CompMs Marry Oaks.NOM Grdgra hdl8y.
1s.Emiuion faGor for TSP Gsatl on Sbck Test ISW Aupuet 20W.PM-10 wt pwl b TSP tlua to AERO IimibBon_
2. Emiasion hctors oMeiwtl tmm APJ2 Satlion 113-&1 k aM SirwWnl Clay Produoh-,Finl sport,Aupua 189].
3. Owomrolhd emisebn feaor for Hydrogen FUorWe Weed on wurw teat wmpWh October 1995.
4. Fuel W.-am'resion hctars obtaiwd imm APJ2 Sion 1.3-Fwl Oil Gm -.-aM NCDEM guidawe.
5. Heat input retire eswmatl to be W,=Btdgalbn for No.21w1 oil end 150,000 Btdpel for No.6 fuel oil.
6. Sulfur=stem of No.2 hel oil assumed W be 0.5%.
2. SulfulcoMentor N1Efwloilaewmed-2.1%.
6. Emission f-11 for Tohl Flwndes b(1.6)4(Hydrogen Flwnda emiuMrn 1acto0.
from APJ2
m NC CAP
n5P
rom AERO

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Table A-4
2016 Air Emissions Inventory
Supporting Emissions Calculations
Formaldehyde Emissions From Natural Gas Combustions In Brick Tunnel Kilns
Triangle Brick Company-Merry Oaks Facility
Fuel Combustion Data
2016 Natural Gas Combusted -Kiln#1: 1,871,000 ft3
2016 Natural Gas Combusted -Kiln#2: 0 ft3
2016 Natural Gas Combusted-Kiln#3: 246,003,000 ft3
Formaldehyde Emission Factor': 0.075 Ib/10e06 ft3
Emission Calculations-Kiln#1
Formaldehyde(lb/yr) = 1871000 ft3 x 0.075 Ib/10e06 ft3
0.14033 lb formaldehyde/yr
Emission Calculations-Kiln#2
Formaldehyde(lb/yr) = 0 ft3 x 0.075 Ib/10e06 ft3
0.00 lb formaldehyde/yr
Emission Calculations-Kiln#3
Formaldehyde(lb/yr) = 246003000 ft3 x 0.075 Ib/10e06 ft3
18.450 lb formaldehyde/yr
Total Formaldehyde Emissions-Kiln#1, Kiln#2,and Kiln#3
Formaldehyde(lb/yr) , = 18.69 Ibs Formaldehyde/yr
1.NCDAQ Natural Gas Combustion Emissions spreadsheet

Table A-5
2016 Air Emissions Inventory
Supporting Emissions Calculations
Emissions From Natural Gas Combustion In Rotary Sand Dryer(SD-1)
Triangle Brick Company-Merry.Oaks Facility
Hours,of operation (hr/ .r) f
Natural Gas"Combusied`W)
Sand,Processed tpvi
Emission Emission L Emiss.on `•
Pollutant Factor 3 =Rate Rate'`
fll
Ib/Hr
Ib
NOX 1 2.24E-06, 9.83E-06
CO 0.84 1.88E-06 8.26E-06
SO2 0.006 1.35E-08 5.90E-08
VOC 0.055 1.23E-07 5.41 E-07
Formaldehyde 0.00075 1.68E-09 7.37E-09
Emission Emission 'Emission',
Pollutant` Factorz:3 Rate Rate
lb/ton`� _ ;.;(Ib/hrj (tpY) ..
PM 0.02 1.64E-03 7.20E-03
PM10 0.02 1 1.64E-03 I 7.20E-03
PM2.5 0.02 1.64E-03 I 7.20E-03
1.NCDAQ Natural Gas Combustion Emissions spreadsheet
2.PM emission factors are from AP-42 Section 11.19.1 "Sand and Gravel Processing".
3.All emission factors are for uncontrolled emissions from a rotary sand dryer.Since unit is
enclosed in building the emission factors have been multiplied by 0.01 to account for control.

Table A-6
Calulation of 2016 Air Emissions from Crushing,Screening,and Grinding Operations
(Source I.D. PC1-PC6 CG1 -CG49)
Triangle Brick Company
9 P Y
Merry Oaks, North Carolina
Emission Annual Actual Actual
Source` Pollutant ; 'Units, 'Throughput Emission` , Emiss"ori
, - . � > .;
tons
e
x ; ' Rat '. Ib/ .r Rate__ton/ r
PM-2,53 5.90E-02 Ibs/ton 192,414 11,352 5.68
Primary Crushing4 PM-10 5.90E-02 Ibs/ton 192,414 11,352 5.68
PM3 5.90E-02 ibs/ton 192,414 11,352 5.68
PM-2.53 0.0023 Ibs/ton 192,414 443 0.22
Grinding &Screening PM-10 0.0023 Ibs/ton 192,414 443 0.22
PM 0.025 Ibs/ton 192,414 4,810 2.41
1. Emission factor based on AP-42 Section 11.3"Brick and Structural Clay Product
Manufacturing,Final Report",August 1997.
2. Throughput based on multiplying fired brick production by 5.0/3.8 to account for moisture content of raw material.
3. PM2.5(and PM for primary crushing)emission factors not included in AP-42.Assumed emission factors=PM,()emission
factor.
4.PM-10 emission factor for primary crushing in AP-42 is based on a test on a primary crusher with a fabric filter control.
Assumed control had 99%efficiency.Triangle Brick's primary crusher has no control,therefore the AP-42 emission factor is
�' divided by(1-.99).

Table A-7
2016 Air Emissions Inventory
Supporting Emissions Calculations
- Natural Gas Combustion Emissions from Brick Tunnel Kilns.
Triangle Brick Company-Merry Oaks Facility
Natural Gas Combusted (without any brick produced)
MOK1 ! 1,871,000 -ft3
MOK2 N/A ft3
MOK3 N/A ft3
Emission,. Emis6i0:Rate {
Pollutant Factor' (Ibs/yr): + 3 Totat MO
(IbL10 ft ): r ,MOK1 MOK2 ,.,MOK3`
NOx 100 187.1 N/A NIA 187.1
CO 84 157.164 N/A NIA 157.164
PM (Total)2 7.6 14.2196 N/A N/A 14.2196
S02 0.6 1.1226 N/A N/A 1.1226
TOC 11 20.581 N/A NIA 20.581
VOC 5.5 10.2905 N/A N/A, 10.2905
Acetaldehyde(H,T)** 0.0000152 0.00003 NIA N/A, 2.84392E-05
Acrolein (H,T)** 0.000018 0.00003 NIA, NIA. 0.000033678
Ammonia(T)** 3.2 5.98720 N/A N/A 5.9872
Arsenic H,T) 0.0002 0.00037 NIA. NIA, 0.0003742
Benzene(H,T) 0.0021 0.00393 NIA N/A 0.0039291
Benzo(a)p rene(H,T) 0.0000012 2.25E-06 N/A NIA 2.2452E-06
Beryllium, H,T) 0.000012 0.000.02 N/A N/A 0.000022452
i
Cadmium (H,T) 0.0011 0.00206 N/A °~aIA, 0.0020581
- Chromium (VI) (H,T) 0.0014 0.00262 N/A NY0.0026194
Cobalt(H) 0.000084 0.00016 NIA, WA, 0.000157164
n-Hexane(H,T) 1.8 3.36780 N/A, NIA. 3.3678
Lead H) 0.0005 0.00094 NIA: NIA 0.0009355
Manganese(H,T) 0.00038 0.00071 N/A N/A 0.00071098
Mercury H,T) 0.00026 0.00049 N/A NIA 0.00048646 .
Napthalene(H) 0.00061 0.00114 N/A N/A 0.00114131
Nickel(H,T) 0.0021 0.00393 N/A NIA, 0.0039291
Selenium H 0.000024 0.00004 N/A NIA, 0.000044904
Toluene H;T 0.0034 0.00636 N/P, NIA 0.0063614
1.NCDAQ Natural Gas Combustion Emissions spreadsheet
2.PM(Total)is assumed to be PM2.5=PM10
I
I

Table A-8
2016 Air Emissions Inventory
Supporting Emissions Calculations
VOC Emissions from Tanks
Triangle Brick Company-Merry Oaks Facility
Annual Throughputs(gallons)
Additive A Tank „ /:" (1 tank)
Gasoline Tank_ %%j `, (1 tank)
Highway Diesel Tank j (1 tank)
No zFuel Oil Tanks (2 tanks)
No.&FuelOil°Tank ,/ (9 tank)
Tanks 4.09d Run Results
Additive A Tank
VOC'(Ibs)'
Components Working Breathing Totala�
Loss Loss Emissions
Calcium Lignosulfonate 307.52 531.99 839.51
Gasoline Tank
VQQ
Components Working,,_ ;, Breathing , Total
` Loss " Loss< Emissions'
GasoI1ne,(RVP`7) 49.76 287.13 336.89
Highway Diesel Tank
VOC("Ibs)
Components Working Breathing Total =
. -
,Loss Loss Emissions
Highway Diesef_ " 4.55- 3.98 8.53
No.2 Fuel Oil Tank 1
-- :VOC(lbs).
Components Working Breathing Total
Loss .Loss ,- Emissions.:
N6.2,Fue101 0.33. 3.98 4.31
No.2 Fuel Oil Tank 2
Components Working L Breathing. Total
Loss. Loss " Emissions.
No.2"Fuel Oil 0.33 3.98 4.31
No.6 Fuel Oil Tank
=VOC,(Ibs)
Components Working Breathing' Total
:Loss ss Emissions."
!No.6 Fuel Oil 0.00. 0.04 0.04

Table A-9
2016 Emissions Summary
Triangle Brick Company
Merry Oaks Facility
Triangle Brick Company
Durham, North Carolina
NC TAP 2016 2016
Pollutant Wor HAP Emissions Emissions
Ib/ r ton/ r
TSP Neither 71,300 35.65
PM-10 Neither 66,932 33.47
SO2 Neither 9,170 4.59
NOx Neither 18,613 9.31
CO Neither 84,535 42.27
TOC Neither 21 0.01
VOC Neither 9,510 4.76
1,1,1 Trichloroethane TAP/HAP 0.69 3.44E-04
1 A Dichlorobenzene TAP/HAP 7.02 3.51 E-03
2-Butanone(MEK) TAP/HAP 32.17 1.61E-02
2-Hexanone (MIBK) TAP/HAP 12.43 6.21E-03
Acetaldehyde TAP/HAP 0.00 1.42E-08
Acetone Neither 248.60 1.24E-01
Acrolein TAP/HAP 0.00 1.68E-08
Ammonia TAP 5.99 2.99E-03
Antimony HAP 9.33 4.66E-03
Arsenic TAP/HAP 3.35 1.67E-03
Benzene TAP/HAP 424.09 2.12E-01
Benzo(a)p rene TAP 0.00 1.12E-09
Beryllium TAP/HAP 0.06 3.07E-05
Bis (2-eth (hex I) Phthalate HAP 292.47 1.46E-01
But Ibenz (phthalate Neither 2.63 1.32E-03
Cadmium TAP/HAP 0.84 4.22E-04
Carbon Disulfide TAP/HAP 6.29 3.14E-03
Chlorine TAP/HAP 190.11 9.51 E-02
Chloroethane HAP 83.35 4.17E-02
Chloromethane HAP 97.98 4.90E-02
Chrome VI TAP/HAP 0.00 0.00E+00
Chromium HAP 3.06 1.53E-03
Cobalt HAP 0.62 3.12E-04
Di Butyl Phthalate HAP 20.47 1.02E-02
Dieth (phthalate Neither 35.10 1.75E-02
Ethyl Benzene HAP 6.43 3.22E-03
Formaldehyde TAP/HAP 18.59 9.30E-03
n-Hexane TAP/HAP 3.37 1.68E-03
Hydrogen Chloride TAP/HAP 16,679.01 8.34E+00
Hydrogen Fluoride TAP/HAP 27,455.95 1.37E+01
lodomethane HAP 13.60 6.80E-03
Lead HAP 21.94 1.10E-02
Manganese TAP/HAP 12.37 6.19E-03
Mercury TAP/HAP 1.46 7.31 E-04
Naphthalene HAP 9.51 4.75E-03
Nickel TAP/HAP 1.88 9.38E-04
Phenol TAP/HAP 12.58 6.29E-03
Pol cyclic Organic Matter TAP 0.00 0.00E+00
Selenium HAP 6.26 3.13E-03
Styrene TAP/HAP 2.92 1.46E-03
Tetrachloroethene TAP/HAP 0.41 2.05E-04
Toluene TAP/HAP 23.40 1.17E-02
Total Fluorides TAP 67,352.94 3.37E+01
X lene TAP/HAP 18.28 9.14E-03

TANK 4.09D RUNS
TRIANGLE BRICK COMPANY-MERRY OAKS

TANKS 4.0 Report Page I of 7
TANKS 4.0.9d
Emissions Report-Detail Format
Tank Indentification and Physical Characteristics
Identification
User Identification: Merry Oaks Additive A Tank
City: Raleigh
State: North Carolina
Company: Triangle Brick Company
Type of Tank: Vertical Fixed Roof Tank
Description:
Tank Dimensions
Shell Height(ft): 30.00
Diameter(ft): 12.00
Liquid Height(ft): 30.00
Avg.Liquid Height(ft): 15.00
Volume(gallons): 25,000.00
Turnovers: 3.86
Net Throughput(gal/yr): 96,608.00
Is Tank Heated(y/n): N
Paint Characteristics
Shell Color/Shade: White/White
Shell Condition Good
Roof Color/Shade: WhiteANhite
Roof Condition: Good
Roof Characteristics
Type: Dome
Height(ft) 0.00
Radius(it)(Dome Roof) 12.00
Breather Vent Settings
Vacuum Settings(psig): -0.03
Pressure Settings(psig) 0.03
Meterological Data used in Emissions Calculations:Raleigh,North Carolina(Avg Atmospheric Pressure=14.53 psia)
file:///C:/Program%2OFiles%20(x86)/Tanks4O9d/summarydisplay.htm 6/6/2017
i

TANKS 4.0 Report Page 2 of 7
TANKS 4.0.9d
Emissions Report-Detail Format
Liquid Contents of Storage Tank
Merry Oaks Additive A Tank-Vertical Fixed Roof Tank
Raleigh,North Carolina
Liquid
Daily Liquid Surf. Bulk Vapor Liquid Vapor
Temperature(deg F) Temp Vapor Pressure(psia) Me[. Mass Mass Me[. Basis for Vapor Pressure
Mixtum[Component Month Avg. Min. Max. (deg F) Avg. Min. Max. Weight F-1. Fract Weight Calculations
Calcium Lignosulfonate All 61.17 55.60 66.73 59.30 0.2529 0.2280 0.2668 528.6100 528.61 Option 1:VP60=.25 VP70=.275
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TANKS 4.0 Report Page 3 of 7
TANKS 4.0.9d
Emissions Report-Detail Format
Detail Calculations (AP-42)
Merry Oaks Additive A Tank-Vertical Fixed Roof Tank
Raleigh,North Carolina
Annual Emission Calcaulations
Standing Losses(Ib): 631.9875
Vapor Space Volume(cu ft): 1,789.5488
Vapor Density(lb/cu it): a.0239
Vapor Space Expansion Factor. 0.0413
Vented Vapor Saturation Factor. 0.8250
Tank Vapor Space Volume:
Vapor Space Volume(cu it): 1,789.5488
Tank Diameter(ft): 120000
Vapor Space Outage(ft): 15.8231
Tank Shell Height(it): 30.0000
Average Liquid Height(ft): 15.0000
Roof Outage(it): 0.8231
Roof Outage(Dame Roof)
Roof Outage(it): 0.8231
Dome Radius(it)- 120000
Shell Radius(it): 6.0000
Vapor Density '
Vapor Density(Ibtcu it): 0.0239
Vapor Molecular Weight(Ibllb-mole): 528.6100
Vapor Pressure at Daily Average Liquid -,
Surface Temperature(psia): 0.2529
Daily Avg.Liquid Surface Temp.(deg.1 520.8354
Daily Average Ambient Temp.(deg.F): 59.2833
Ideal Gas Constant R
(psla cult/(lbmol-deg R)): 10.731
Liquid Bulk Temperature(deg.R): 518.9733
Tank Paint Solar Absorptance(Shell): 0.1700
Tank Paint Solar Absorptance(Roof): 0.1700
Daily Total Solar Insulation
Factor(Stu/sgft day): 1.393,0797
Vapor Space Expansion Factor
Vapor Space Expansion Factor. 0.0413
Dairy Vapor Temperature Range(deg.1 22.2671
Daily Vapor Pressure Range(paia): 0.0388
Breather Vent Press.Setting Range(psia): 0.0600
Vapor Pressure at Daily Average Liquid
Surface Temperature(psia): 0.2529
Vapor Pressure at Daily Minimum Liquid
Surface Temperature(psia): 0.2280
Vapor Pressure at Daily Maximum Liquid
Surface Temperature(psla): 02688
Daily Avg.Liquid Surface Temp.(deg R): 520.8354
Daily Min.Liquid Surface Temp.(deg R): 515.2687
Daily Max.Liquid Surface Temp.(deg R): 526.4022
Daily Ambient Temp.Range(deg.R): 21.7167
Vented Vapor Saturation Factor
Vented Vapor Saturation Factor. 0.8250
Vapor Pressure at Daily Average Liquid:
Surface Temperature(psia): 0.2529
Vapor Space Outage(it): 15.8231
Working Losses(Ib): 307.5186
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TANKS 4.0 Report Page 4 of 7
Vapor Molecular Weight(IMb-mole): 52B.6100
Vapor Pressure at Daily Average Liquid
Surface Temperature(psia): 0.2529
Annual Net Throughput(gal/yr.): 96,608.0000
Annual Turnovers: 3.8643 '
Turnover Factor. 1.0000
Maximum Liquid Volume(gal): 25,000.0000
Maximum Liquid Height(ft): 30.0000
Tank Diameter(ft): 12.0000
Working Loss Product Factor: 1.0000
Total Losses(lb): 839.5051
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TANKS 4.0 Report Page 5 of 7
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TANKS 4.0 Report Page 6 of 7
TANKS 4.0.9d
Emissions Report-Detail Format
Individual Tank Emission Totals
Emissions Report for:Annual
Merry Oaks Additive A Tank-Vertical Fixed Roof Tank
Raleigh,North Carolina
Losses(lbs)
Components Working Loss I Breathing Loss Total Emissions
Calcium Lignosulfonate 307.52 531.99 839.51
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TANKS 4.0 Report Page 7 of 7
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TANKS 4.0 Report Page 1 of 7
TANKS 4.0.9d
Emissions Report-Detail Format
Tank Indentification and Physical Characteristics
Identification
User Identification: Merry Oaks Gasoline Tank
City: Raleigh
State: North Carolina
Company: Triangle Brick Company
Type of Tank: Vertical Fixed Roof Tank
Description:.
Tank Dimensions
Shell Height(ft): 18.00
Diameter(ft): 5.50
Liquid Height(ft): 18.00
Avg.Liquid Height(ft): 9.00
Volume(gallons): 3,000.00
Turnovers: 2.58
Net Throughput(gal/yr): 7,741.00
Is Tank Heated(y/n): N
Paint Characteristics
Shell Color/Shade: Gray/Light
Shell Condition Good
Roof Color/Shade: Gray/Light
Roof Condition: Good
Roof Characteristics
Type: Dome
Height(ft) 4.00
Radius(ft)(Dome Roof) 5.50
Breather Vent Settings
Vacuum Settings(psig): -0.03
Pressure Settings(psig) 0.03
Meterological Data used in Emissions Calculations:Raleigh,North Carolina(Avg Atmospheric Pressure=14.53 psia)
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TANKS 4.0 Report Page 2 of 7
TANKS 4.0.9d
Emissions Report-Detail Format
Liquid Contents of Storage Tank
Merry Oaks Gasoline Tank-Vertical Fixed Roof Tank
Raleigh,North Carolina
Uquitl
Daily Liquid Surf. Bulk Vapor Liquid Vapor
Temperature(deg F) Temp Vapor Pressure(psia) Mol. Mass Mass Mol. Basis for Vapor Pressure
Modure/Component Month Avg. Min. Max. (deg F) Avg Min. Max. Weight Frect. F—L Weight Calculations
Gasoline(RVP 7) All 66.48 67.31 75.66 61.52 3.9699 3.2977 4.7489 68.0000 92.00 Option 4:RVP=7,ASTM Slope=3
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TANKS 4.0 Report Page 3 of 7
TANKS 4.0.9d
Emissions Report-Detail Format
Detail Calculations(AP-42)
Merry Oaks Gasoline Tank-Vertical Fixed Roof Tank
Raleigh,North Carolina
Annual Emission Calcaulations
Standing Losses(lb): 287.1344
Vapor Space Volume(curft): 294.8516
Vapor Density(lb/cu ft): 0.0478
Vapor Space Expansion Factor: 0.2015
Vented Vapor Saturation Factor. 0.2769
Tank Vapor Space Volume:
Vapor Space Volume(cu ft): 294.8516
Tank Diameter(fq: 6.5000
Vapor Space Outage(ft): 12.4105
Tank Shell Height(ft):. 18.0000
Average Liquid Height(ft): 9.0000
Root Outage(ft): 3.4105
Roof Outage(Dome Roof)
Roof Outage(ft): 3.4105
Dome Radius(it): 5.5000
Shell Radius(ft): 2.7500
d Vapor Density
Vapor Density(Ib/cu ft): 0.0478
Vapor Molecular Weight(IbAb-mole): 68.0000
Vapor Pressure at Daily Average Liquid
Surface Temperature(psia): 3.9699
Daily Avg.Liquid Surface Temp.(deg.R): 526.1506
Daily Average Ambient Temp.(deg.F): 59.2833
Ideal Gas Constant
(psis cult/Ut-ol-deg R)): 10.731
Liquid Bulk Temperature(deg.R): 521:1933
Tank Paint Solar Absorptance(Shell): 0.5400
Tank Paint Solar Absorptance(Roof): 0.5400
Daily Total Solar Insulation
Factor(Btufsgft day): 1,393.0797
VaporSpace Expansion Factor
Vapor Space Expansion Factor. 0.2015
Daily Vapor Temperature Range(deg,R): 35.6994
Daily Vapor Pressure Range(Pala): 1.4513
Breather Vent Press.Setting Range(psia): 0.0600
Vapor Pressure at Daily Average Liquid
Surface Temperature(psia): 3.9699
Vapor Pressure at Daily Minimum Liquid
Surface Temperature(psia): 3.2977
Vapor Pressure at Daily Maximum Liquid
Surface Temperature(psia): 4.7489
Daily Avg.Liquid Surface Temp.(deg R): 526.1506
Daily Min.Liquid Surface Temp.(deg R): 516.9758
Daily Max.Liquid Surface,Temp.(deg R): 535.3255 -
Rally Ambient Temp.Range(deg.R): 21.7167
Vented Vapor Saturation Factor
Vented Vapor Saturation Factor. 0.2769
Vapor Pressure at Daily Average Liquid:
Surface Temperature(psia): 3.9699
Vapor Space Outage(ft): IZ4105
Working Losses(lb): 49.7552
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TANKS 4.0 Report Page 4 of 7
Vapor Molecular Weight(IEAbmole): 68.0000
Vapor Pressure at Daily Average Liquid
Sudece Temperature(psia): 3.9699
Annual Net Throughput(gallyr): 7,741.0000
Annual Turnovers: 2.5803
Turnover Factor. 1.0000
Maximum Liquid Volume(gal): 3,000.0000
Maximum Liquid Height(it): 18.0000
Tank Diameter(it): 5.5000
Working Loss Product Factor. 1.0000
Total Losses(Ib): 336.8897
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TANKS 4.0 Report Page 5 of 7
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TANKS 4.0 Report Page 6 of 7
TANKS 4.0.9d
Emissions Report-Detail Format
Individual Tank Emission Totals
Emissions Report for:Annual
Merry Oaks Gasoline Tank-Vertical Fixed Roof Tank
Raleigh,North Carolina
Losses(lbs)
Components Working Loss I Breathing Loss Total Emissions
Gasoline(RVP 7) 49.76 287.13 336.89
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TANKS 4.0 Report Page 7 of 7
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TANKS 4.0 Report Page 1 of 7
TANKS 4.0.9d
Emissions Report-Detail Format
Tank Indentification and Physical Characteristics
Identification
User Identification: Merry Oaks Highway Diesel Tank
City: Raleigh
State: North Carolina
Company: Triangle Brick Company
Type of Tank: Vertical Fixed Roof Tank
Description:
Tank Dimensions
Shell Height(ft): 30.00
Diameter(ft): 12.00
Liquid Height(ft): 30.00
Avg.Liquid Height(ft): 15.00
Volume(gallons): 25,000.00
Turnovers: 8.66
Net Throughput(gal/yr): 216,397.00
Is Tank Heated(y/n): N
Paint Characteristics
Shell Color/Shade: White/White
Shell Condition Good
Roof Color/Shade: White/White
Roof Condition: Good
Roof Characteristics
Type: Dome
Height(ft) 0.00
Radius(ft)(Dome Roof) 12.00
Breather Vent Settings
Vacuum Settings(psig): -0.03
Pressure Settings(psig) 0.03
Meterological Data used in Emissions Calculations:Raleigh,North Carolina(Avg Atmospheric Pressure=14.53 psia)
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TANKS 4.0 Report Page 2 of 7
TANKS 4.0.9d
Emissions Report-Detail Format
Liquid Contents of Storage Tank
Merry Oaks Highway Diesel Tank-Vertical Fixed Roof Tank
Raleigh,North Carolina
Liquid
Daily Liquid Surf. Bulk Vapor Liquid Vapor
Temperature(deg F) Temp Vapor Pressure(psia) Mol. Mass Mass M.I. Basis for Vapor Pressure
Mixture/Componerd Month Avg. Min. Max. (deg F) Avg. Min. Max. Weight Fract Fract Weight Calculations
Distillate fuel oil no.2 All 61.17 55.60 66.73 59.30 0.0066 0.0056 0.0082 130.0000 188.00 Opbon 1:VP60=.0065 VP70=.009
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TANKS 4.0 Report Page 3 of 7
TANKS 4.0.9d
Emissions Report-Detail Format
Detail Calculations(AP-42)
Merry Oaks Highway Diesel Tank-Vertical Fixed Roof Tank
Raleigh,North Carolina
Annual Emission Calcauladons
Standing Losses(lb): - 3.9805
Vapor Space Volume(cu it): 1,789.5488
Vapor Density(Ib/cu ft): 0.0002
Vapor Space Expansion Factor. 0.0388
Vented Vapor Saturation Factor. 0.9943
Tank Vapor Space Volume:
Vapor Space Volume(cu Ity 1,789.5488
Tank Diameter(ft): 120000
Vapor Space Outage(it): 15.8231
Tank Shell Height(ft): 30.0000
Average liquid Height(ft): 15.0000
Roof Outage(ft): 0.8231
Roof Outage(Dome Roof)
Roof Outage(ft): 0.8231
Dome Radius(ft): 120000
Shell Radus(ft): 6.0000
Vapor Density
Vapor Density(Ib/cu ft): 0.0002
Vapor Molecular Weight(Ibgbmole): 130.0000
Vapor Pressure at Daily Average Liquid
Surface Temperature(psia): 0.0068
Daily Avg.Liquid Surface Temp.(deg.R): 520.8354
Daily Average Ambient Temp.(deg.F): 59.2833
Ideal Gas Constant R
(psis cult y(lb-mol-deg R)): 10.731
Liquid Bulk Temperature(deg.R): 518.9733
Tank Paint Solar Absorptance(Shell): 0.1700
Tank Paint Solar Absorptance(Roof): 0.1700
Daily Total Solar Insulation
Factor(Stu/sgft day): 1,393.0797
Vapor Space Expansion Factor
Vapor Space Expansion Factor: Q0388
Daily Vapor Temperature Range(deg.R): 22.2671
Daily Vapor Pressure Range(psis): 0.0026
Breather Vent Press.Setting Range(psia): 0.0600
Vapor Pressure at Daily Average Liquid
Surface Temperature(psi.): 0.0068
Vapor Pressure at Daily Minimum Liquid
Surface Temperature(psis): 0.0056
Vapor Pressure at Daily Maximum Liquid
Surface Temperature(Pala): 0.0062
Daily Avg.Liquid Surface Temp.(deg R): 520.8354
Daily Min.Liquid Surface Temp.(deg R): 515.2687
Daily Max.Liquid Surface Temp.(deg R): 526.4022
Daily Ambient Temp.Range(deg.R): 21.7167
Vented Vapor Saturation Factor
Vented Vapor Saturation Factor. 0.9943
Vapor Pressure at Daily Average Liquid:
Surface Temperature(psia): 0.0068
Vapor Space Outage(ft): 15.8231
Working Losses(lb): 4.5489
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TANKS 4.0 Report Page 4 of 7
Vapor Molecular Weight(Ihlibmole): 130.0000
Vapor Pressure at Daily Average Liquid
Surface Temperature(psia): 0.0068
Annual Net Throughput(gatfyr.): 216,397.0000
Annual Turnovers: 8.6559
Turnover Factor. - 1.0000
Maximum Llquid Volume(gap: 25,000.0000
Maximum Liquid Height MY30.0000
Tank Diameter(ft): 12.0000
Working Loss Product Factor: 1.0000
Total Losses()h): 8.5293
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TANKS 4.0 Report Page 5 of 7
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TANKS 4.0 Report Page 6 of 7
TANKS 4.0.9d
Emissions Report-Detail Format
Individual Tank Emission Totals
Emissions Report for:Annual
Merry Oaks Highway Diesel Tank-Vertical Fixed Roof Tank
Raleigh,North Carolina
Losses(lbs)
Components Working Loss r- Breathing Loss I Total Emissions
Distillate fuel oil no.2 4.55 --3.981 8.53
f
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TANKS 4.0 Report Page 7 of 7
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TANKS 4.0 Report Page 1 of 6
TANKS 4.0.9d
Emissions Report-Detail Format
Tank Indentification and Physical Characteristics
Identification
User Identification: Merry Oaks No.2 Fuel Oil Tank 1
City: Raleigh
State: North Carolina
Company Triangle Brick Company
Type of Tank Vertical Foxed Roof Tank
Description:
Tank Dimensions
Shell Height(ft): 30.00
Diameter(it): 1200
Liquid Height(ft): 30.00
Avg.Liquid Height(ft): 15.00
Volume(gallons): 25,000.00
Turnovers: 0.62
Net Throughput(gaVyr): 15,500.00
IS Tank Heated(y/n): N
Paint Characteristic.
Shell Co cdShade: WNteANnfte
Shell Condition Good
Roof ColodShade: WhiteAMtite
Roof Condition: Good
Root Characteristics
Type: Dome
_ Height(R) 0.00
Radius(ft)(Dome Roof) 1200
Breather Vent Settings
Vacuum Settings(psig): -0.03
Pressure Settings(psig) 0.03
Meterological Data used in Emissions Calculations:Raleigh,North Carolina(Avg Atmospheric Pressure=14.53 psia)
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TANKS 4.0 Report Page 2 of 6
TANKS 4.0.9d
Emissions Report-Detail Format
Liquid Contents of Storage Tank
Merry Oaks No.2 Fuel Oil Tank 1-Vertical Fixed Roof Tank
Raleigh,North Carolina
wpm
�rfaausaf. vane. vaaor
Temper�re(Oep F) Tem.pp Vapor Fimve(pcm) MM Mass Mass Bass luVapor P.
NhaaeTompmad MmM Avp. MIO Mac (aW F) Avy Mhc Ma N4g11 Free Fret Va!gI.Il:f
O'uEAala Mel pAnn 2 AO .1.17 5Sfi0 W.73 S9.3O O.M 0.0 O.0002 13O= 18000 o;l 1:VFNI=.DaS Vp]O=.IX9
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TANKS 4.0 Report Page 3 of 6
TANKS 4.0.9d
Emissions Report-Detail Format
Detail Calculations(AP-42)
Merry Oaks No.2 Fuel Oil Tank t-Vertical Fixed Roof Tank
Raleigh,North Carolina
Annual EL-LalmuMliom
abneuq Las®(W): 3.9 8
Vapaspam Volume([u N 6a5ae6: 1,]
Vapor Smarty apa naom
Vapor&pace FimnsMn Fatlw. 00366
VeaeR Vapor 63hJaaan Fatlor, a99a3
Tan.. Gam—a:
Vapr Space VW ane(al): 1,)6¢5a6n
1m.Gbmeler0): I2¢an
.-saace ONape(M: ,5623,
TanN9RL XeipM(fl): 30.W00
Avempe u 11epM lN: 151Do0
RmIIARa1.Oe CN): ¢62J1
RMQGape(G[me Roo)
Rao!Gaaw,(flR ¢02J1
Gana Rams MY 12n0o0
..a R.—M: aW00
Vaa.Gem.y
Vapor—.Y(.wn): n6ar2
Vapor Na'ttularNtlpM(161E+nox): 130.0000
S.K
Vapor..T. ffiGordy Average L'quM
,Yan TempaaWm lmb): ¢=4
GailY Avp.ga suRaaT (%FR): 52n&35a
I-IGaaG.AmaMnl Tung(Reg F): 59.26'fJ
IReal Gaa Gan5aniR
(Pb eel/ mol-0e0 R)): 10.]31
UeuM BURTemmmtum(Rm.R): 51a
0.]n0.17w
TanN PdIM sale Panryanm(6MIq:
TeNI PavV SobrAtr.,apb�(Rool): 0.1700
Gordy Total Solar lRSWatlai
Fetlor(elw5afl RdY): 1,39].0I J]
Vapor apam Eapambn Fatlu
wwspaa Eap o.Fa—. n¢'i6B
Dal YVaW.,apa—Ra-0.a Rl: 32.2NT1
Gaily Vapor Pmsae Ra G(Ps): 0.0026
&n) V-Rana—!VRapelpaia): 0.0500
Vapor Presae ffi D.,AvaaO a Lq W R
salam Te a aaaoe(ptia): 0.nO6B
Va,araaaT —e M'emnum lBCWR
Swam TempaaSRe(pab): a0056
Vapor PresT ffiGaily(P a):um liauM
aortae Tanpemeae(T- ,—
GalYAvgUpwRSe—Ta (ReDR). s's2 W
�Jy Mlrt L1q-Stabm Tan0.(Rc51 RI: 51526�
DaIY Mai LIquM Salim T.P.(Re0 R): 526.
Galy—.Tarp Rape(Reg R): 21.1W]I61
v—Vapasahaalbn Fatly
VenMRVapt$aladaOn Fatlor, n00a3
Vapor Pasure et 0.adYAvaaOe Uc M:
swam TempaeWre(pva): Horse
Vapor Spam GWape(M: 156rl1
V. gLoran(W): a3256
Vapor Mo. .mw(W .,a): 130A000
Vapor Ppsae ffiMV Aye2¢e L4q
suRam Tem aa.(p.Y a006B
Annual Net T.mm.pul(g.*,): 15,500.0000
An—ITamvae: o.6100
Tumor F...[ L—
MaMum UauM Volume(pa0: 25...W00
T.Rman UauMXeipM()): 3n0o00
Tank ObmHer(10: 1].0000
'MiMnp Lola Prmucl Fatlw 1.0000
Total Lose(1e): l]063
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TANKS 4.0 Report Page 4 of 6
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TANKS 4.0 Report Page 5 of 6
TANKS 4.0.9d
Emissions Report-Detail Format
Individual Tank Emission Totals
Emissions Report for:Annual
Merry Oaks No.2 Fuel Oil Tank 1-Vertical Fixed Roof Tank
Raleigh,North Carolina
Losses(16s)
Components Worfdng Loss &eafhin9 Lass Total Emissions
0istiilate fuel all no.2 0.33113.98 4.31
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TANKS 4.0 Report Page 6 of 6
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TANKS 4.0 Report Page 1 of 7
TANKS 4.0.9d
Emissions Report-Detail Format
Tank Indentification and Physical Characteristics
Identification
User Identification: Merry Oaks No.2 Fuel Oil Tank 2
City: Raleigh
State: North Carolina
Company: Triangle Brick Company
Type of Tank: Vertical Fixed Roof Tank
Description:
Tank Dimensions
Shell Height(ft): 30.00
Diameter(ft): 12.00
Liquid Height(ft): 30.00
Avg.Liquid Height(ft): 15.00
Volume(gallons): 25,000.00
Turnovers: 0.62
Net Throughput(gal/yr): 16,600.00
Is Tank Heated(y/n): N
Paint Characteristics
Shell Color/Shade: WhiteAAlhite
She Condition Good
Roof Color/Shade: White/White
Roof Condition: Good
Roof Characteristics
Type: Dome
Height(ft) 0.00
Radius(ft)(Dome Roof) 12.00
Breather Vent Settings
Vacuum Settings(psig): -0.03
Pressure Settings(psig) 0.03
Meterological Data used in Emissions Calculations:Raleigh,North Carolina(Avg Atmospheric Pressure=14.53 psia)
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TANKS 4.0 Report Page 2 of 7
TANKS 4.0.9d
Emissions Report-Detail Format
Liquid Contents of Storage Tank
Merry Oaks No.2 Fuel Oil Tank 2-Vertical Fixed Roof Tank
Raleigh,North Carolina
Liquid
Daily Liquid Surf. Bulk Vapor Liquid Vapor
Temperature(deg F) Temp Vapor Pressure(psia) M.I. Mass Mass Mol. Basis for Vapor Pressure
Mixture/Component Month An Min. Max. (deg F) Avg. Mn. Max. Weight. FracL FracL Weight Calculations
Distillate fuel ail no.2 All 61.17 55.60 65.73 59.30 0.0068 0.0056 0.0082 130.0000 168.00 Option 1:VP60=.0065 VP70=.009
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TANKS 4.0 Report Page 3 of 7
TANKS 4.0.9d
Emissions Report-Detail Format
Detail Calculations (AP-42)
Merry Oaks No.2 Fuel Oil Tank 2-Vertical Fixed Roof Tank
Raleigh,North Carolina
Annual Emission Calcaulabons
Standing Losses(Ib): 3.9805
Vapor Space Volume(cu ft): 1.789.5488
Vapor Density(lb/cu it): 0.0002
Vapor Space Expansion Factor. 0.0388
Vented Vapor Saturation Factor. 0.9943
Tank Vapor Space Volume:
Vapor Space Volume(cu ft): 1,789.5488
Tank Diameter(tt): 120g00
Vapor Space Outage(it): 15.8231
Tank Shell Height(ft): 30.0000
Average Liquid Height(ft): 15.0000
Roof Outage(ft): 0.8231
Roof Outage(Dome RooQ
Roof Outage(it): 0.8231
Dome Radius(ft): 12.0000
Shell Radius(ft): 6.0000
Vapor Density
Vapor Density(Ib/cu ft): 0.0002
Vapor Molecular Weight(Itolb-male): 130.0000
Vapor Pressure at Daily Average Liquid _
Sudace Temperature(psi.): 0.0068
Daily Avg.Liquid Surface Temp.(deg.R): 520.8354
Daily Average Ambient Temp.(deg.F): 59.2833
Ideal Gas Constant R -
(psia cuft!(Ibmol-deg R)): 10.731
Liquid Bulk Temperature(deg.R): 518.9733
Tank Paint Solar Absorptance(Shell): 0.1700
Tank Paint Solar Absorptance(Roof): 0.1700
Daily Total Solar Insulation
Factor(Stulsgft day): 1.393.0797
Vapor Space Expansion Factor
Vapor Space Expansion Factor: - 0.0388
Daily Vapor Temperature Range(deg.R): 22.2671
Daily Vapor Pressure Range(psia): 0.0026
Breather Vent Press.Setting Range(psia): 0.0600
Vapor Pressure at Daily Average Liquid
Surface Temperature(psia): 0.0068
Vapor Pressure at Daily Minimum Liquid
Surface Temperature(psia): 0.0056
Vapor Pressure at Daily Maximum Liquid
Surface Temperature(mla): 0.0002
Daily Avg.Liquid Surface Temp.(deg R): 520.8354
Daily Min.Liquid Surface Temp.(deg R): 515.2687
Daily Max.Liquid Surface Temp.(deg R): 526.4022
Daily Ambient Temp.Range(deg.R): 21.7167
Vented Vapor Saturation Factor
Vented Vapor Saturation Factor. 0.9943
Vapor Pressure at Daffy Average Liquid:
Surface Temperature(psia): 0,0068
Vapor Space Outage(it): 15.8231
Working Losses(lb): 0.3258
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TANKS 4.0 Report Page 4 of 7
Vapor Molecular Weight(Ibnb-mole): 130.0000
Vapor Pressure at Daily Average squid
Surface Temperature(psia): 0.0068
Annual Net Throughput(gavyc): 16.500.0000
Annual Tumovers: 0.6200
Turnover Factor. 1.0000
Ma>omum Liquid Volume(gal): 25,000.0000
Maldmum Liquid Height(it): 30.0000
Tank Diameter(ft): 120000
Working Loss Product Factor. 1.0000
Taal Losses(lb): 4.3063
�t
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TANKS 4.0 Report Page 6 of 7
TANKS 4.0.9d
Emissions Report-Detail Format
Individual Tank Emission Totals
Emissions Report for:Annual
Merry Oaks No.2 Fuel Oil Tank 2-Vertical Fixed Roof Tank
Raleigh,North Carolina
Losses(lbs)
Components Working Loss Breathing Lossl I Total Emissions
Distillate fuel oil no.2 0.33 3.98 4.31
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TANKS 4.0 Report Page 7 of 7
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TANKS 4.0 Report Page 1 of 7
TANKS 4.0.9d
Emissions Report-Detail Format
Tank Indentification and Physical Characteristics
Identification
User Identification: Merry Oaks No.6 Fuel Oil Tank
City: Raleigh
State: North Carolina
Company:
Type of Tank: Vertical Fixed Roof Tank
Description:
Tank Dimensions
Shell Height(ft): 30.00
Diameter(ft): 12.00 -
Liquid Height(ft): 30.00
Avg.Liquid Height(ft): 15.00
Volume(gallons): 25,000.00
Turnovers: 0.00
Net Throughput(gal/yr): 0.00
Is Tank Heated(y/n): N
Paint Characteristics
Shell Color/Shade: White/White
Shell Condition Good
Roof Color/Shade: White/V1lhite
Roof Condition: Good
Roof Characteristics
Type: Dome
Height(ft) 0.00
Radius(ft)(Dome Roof) 12.00
Breather Vent Settings
Vacuum Settings(psig): -0.03
Pressure Settings(psig) 0.03
Meterological Data used in Emissions Calculations:Raleigh,North Carolina(Avg Atmospheric Pressure=14.53 psia)
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TANKS 4.0 Report Page 2 of 7
TANKS 4.0.9d
Emissions Report-Detail Format
Liquid Contents of Storage Tank
Merry Oaks No.6 Fuel Oil Tank-Vertical Fixed Roof Tank
Raleigh,North Carolina
Liquid
Daily Liquid Surf. Bulk Vapor Liquid Vapor
Temperature(deg F) Temp Vapor Pressure(psia) Mol. Mess Mass Mol. Basis for Vapor Pressure
Mlxture(Cumponent Month Avg. Min. Max. (deg F) Avg. Min. Max. Weight Fract Fract Weight Calculations
Residual oil no.6 All 61.17 55.60 66.73 59.30 0.0000 0.0000 0.0001 190.0000 307.00 Option 1:VP60=.00004 VP70=.00006
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TANKS 4.0 Report Page 3 of 7
TANKS 4.0.9d
Emissions Report-Detail Format
Detail Calculations(AP-42) .
Merry Oaks No.6 Fuel Oil Tank-Vertical Fixed Roof Tank
Raleigh,North Carolina
Annual Emission Calcaulations
Standing Losses(Iby 0.0363
Vapor Space Volume(cu ft): 1,789.5488
Vapor Density(lb/cu ft): 0.0000
Vapor Space Expansion Factor. 0.03"
Vented Vapor Saturation Factor. 1.0000
Tank Vapor Space Volume:
Vapor Space Volume(cu ft): 1.789.5488
Tank Diameter(ft): 120000
Vapor Space Outage(ft): 15.8231
Tank Shell Height(it): 30.0000
Average liquid Height(ft): 15.0000
Reof Outage(ft): 0.8231
Roof Outage(Dome Roof)
Roof Outage(it): 0.8231
Dome Radius(ft): 12.0000
Shell Radius(ft): 6.0000
Vapor Density
Vapor Density(Ib)cu ft): 0.0000
Vapor Molecular Weight(IbAb.mcle): 190.0000
Vapor Pressure at Daily Average Liquid
Surface Temperature(psia): 0,0000
Daily Avg.Liquid Surface Temp.(deg.R): 520.8354
Daily Average Ambient Temp.(deg.F): 59.2833
Ideal Gas Constant R
(peia cult/(lb.mol-deg R)): 10.731
Liquid Bulk Temperature(deg.R): 518.9733
Tank Paint Saler Absorptance(Shell): 0.1700
Tank Paint Solar Absorptance(Roof): 0.1700
Daily Total Solar Insulation
Factor(Btufsgft day): 1,393.0797
Vapor Space Expansion Factor
Vapor Space Expansion Factor. 0.0388
Daily Vapor Temperature Range(deg.R): 22.2671
Daily Vapor Pressure Range(psa): a'0000
Breather Vent Press.Setting Range(psia): 0.0600
Vapor Pressure at Daily Average Liquid
Surface Temperature(psia): 0.0000
Vapor Pressure at Daily Minimum Liquid
Surface Temperature(psla): 0.0000
Vapor Pressure at Daily Maximum Liquid
Surface Temperature(psis): 0.0001
Daily Avg.Liquid Surface Temp.(deg R): 520.8354
Daily Min.Liquid Surface Temp.(deg R): 515.2687
Daily Msx.Liquid Surface Temp.(deg R): 528.4022
Daily Ambient Temp.Range(deg.R): 21.7167
Vented Vapor Saturation Factor
Vented Vapor Saturation Factor. 1.0000
Vapor Pressure at Daily Average liquid:
Surface Temperature(psia): 0.0000
Vapor Space Outage(ft): 15.8231
Working Losses(lb): 0.0000
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TANKS 4.0 Report Page 4 of 7
Vapor Molecular Weight(IbORmole): 190.0000
Vapor Pressure at Daily Average Liquid
Surface Temperature(psia): 0.0000
Annual Net Throughput 0.0000
Annual Turnovers: 0.0000
Turnover Factor. 1.0000
Maximum Liquid Volume(gal): 25,000.0000
Maximum Liquid Height(it): 30.0000
Tank Diameter(ft): 12.0000
Working Lose Product Factor. 1.0000
Total Losses(lb): 0.0363
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TANKS 4.0 Report Page 6 of 7
TANKS 4.0.9d
Emissions Report-Detail Format
Individual Tank Emission Totals
Emissions Report for:Annual
Merry Oaks No-..6 Fuel Oil Tank-Vertical Fixed Roof Tank
Raleigh;North Carolina
Losses(Ihs)
Components _ Working Loss Breathing Loss Total Emissions
Residual oil no.6- - - -0.00 0.04 0.0411
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TANKS 4.0 Report Page 7 of 7
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