AQ_F_1900077_20150629_EI_Cmb-EI-File

20 t4 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 YES
NO
Initial Review/Data Entry
0 Enter date received into ED. Date Received: l0.22 20l5
0 Assigned to appropriate individual. Date Assigned: <2P-29-;Z0 Date Due: 10-/$-Zc5/$
❑ Paper copy submitted: One copy received with supporting documentation,certification form signed by responsible official,and
appears generally complete;OR
0 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.
,EJ 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.
1f Check if SCC codes for each OS are accurate and update if needed.
13 Evaluate"U"sources for significance and address according to policy.
0 Calculations/forms appear to add up correctly.
0 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).
0 Check all ED QA/QC reports.
0 Comparison with previous emission inventory must be made and outliers(> 10%)must be investigated and explained.
B 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: /O-!,o-20/S Signature:
Date Submitted to EI Coordinator: id-A - W/5
Date Approved: Initials:

Facility Total CY 2014 Emission Summary Recorded in ED Facility ID #: 1900077
k
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 2014 CY 2013 Demini- %
from ED from Fees mus Change
CO CO 38.60 39.31 0.5 -1.8%
NOx NOx 8.54 8.60 Q.5 -0.7%
PM(TSP) TSP 31.41 32.06 0.5 -2.0%
PM10 PM10 24.08 24.58 0.5 -2.0%
PM2.5 PM2,5 24.07 24.58 0.5 -2.1%
S02 S02 4.30 4.27 0.5 0.7%
VOC Voc 4.99 4.66 0.5 7.2%
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPS) (Pounds/Year)
Pollutant CAS CY 2014 CY 2013 Demini- %
from ED from Fees mus Change
Antimony & Compounds(total mass, inc elemental SB) 8.51 8.69 10.0 -2.1
Antimony Metal- (Component of SBC) 7440-36-0 0.017530 Not 10.0 N/A
Reported
Antimony Unlisted Compounds- Specify Compound SBC-other 8.49 8.69 10.0 -2.3%
(Component of SBC)
Arsenic& Compounds(total mass of elemental AS, arsine and 3.06 3.12 0,01 I -1.9%
all inorganic compounds)
Arsenic Metal, elemental, unreacted(Component of 7440-38-2 0.008350 Not 0.01 N/A
ASC) Reported
Arsenic Unlisted Compounds- Specify Compound ASC-Other 3.05 3.12 0.01 -2.3%
(Component of ASC)
10/06/2015 Pagel of 4

ry
Facility Total CY 2014 Emission Summary Recorded-in ED Facility ID #: 1900077 d
Facility Name: Triangle Brick Company-MeM Oaks Permit#(s): 06897TIO
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPS) (Pounds/Year)
Pollutant CAS CY 2014 CY 2013 Demini- %
from ED from Fees mus Change
Beryllium& compounds(Total mass) 0.057280 0.057220 1.0 0.1%
Beryllium Metal (unreacted) (Component of BEC) 7440-41-7 0.057250 0.057220 1.0 0.1%
Beryllium Unlisted Compounds- Specify Compound BEC-other 0.000030 Not 1.0 N/A
(Component of BEC)- Reported
Cadmium& compounds(total mass includes elemental metal) 0.776120 0.784740 0.1 I -1.1%
Cadmium Metal, elemental,unreacted(Component 0440-43-9 0.776120 0.784740 0.1 -1.1%
CDC)
Chromium-All/Total(includes Chromium (VI) categories, 2.83 Z85 0.1 0.7%
metal and others)
Chromium(VI)Non-Specific Unlisted Compounds- NSCR6-other 0.011490 Not 0.01 N/A
Specify Compound(Component of NSCR6 & CRC) Reported
Chromium Unlisted Compounds- Specify CompoundCRC-other 2.82 2.85 0.1 -1.1%
(Component of CRC)
Chromium(VI)Non-Specific Compounds, as Chrom(VI) 0.011490 Not 0.01 N/A
(Component CRC) Reported "
Chromium(VI)Non-Specific Unlisted Compounds- NSCR6-Other 0.011490 Not 0.01 NIA
Specify Compound(Component of NSCR6 &CRC) Reported
Cobalt& compounds 0.569670 0.581740 1,0 -2.1%
Cobalt Unlisted Compounds- Specify Compound COC-Other 0.569670 0.581740 1.0 -2.1%
(Component of COC)
Lead& compounds 20.01 20.44 1.0 I -2.1%
Lead Unlisted Compounds- Specify Compound PBC-other 20.01 20.44 10.0 -2.1%
(Component of PBC)
Manganese & compounds 11.29 11.53 10.0 -2.1%
Manganese Unlisted Compounds- Specify CompouncIANC-Other 11.29 11.53 10.0 -2.0%
(Component of MNC)
Mercury & Compounds-all total mass includes Hg Vapor 1.34 1.36 0.001 I -1.5%
Mercury,vapor(Component of HGC) 7439-97-6 1.34 1.36 0.001 -2.0%
Nickel& Compounds, sum total mass includes elemental 1.80 1.74 1.0 13.4%
10/06/2015 Page 2 of 4

Facility Total CY 2014 Emission Summary Recorded in ED Facility ID#: 1900077
Facility Name: Triangle Brick Company-Megy Oaks Permit#(s): 06897T10
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPs) (Pounds/Year)
Pollutant CAS CY 2014 CY 2013 Demini- %
from ED from Fees mus Change
Nickel metal (Component of NIC) 7440-02-0 1.80 . 1.74 1.0 3.0%
Polycyclic Organic Matter(7 PAH Compounds for NIF) 0.000000 Not 1.0 I N/A
Reported
Benzo(a)pyrene (Component of 83329/POMTV& 50-32-8 0.000000 Not 1.0 N/A
56553/7PAH) Reported
Polycyclic.Organic Matter(Specific Compounds from OAQPS 8.67 8.86 1.0 -2.1
or Tip
Benzo(a)pyrene(Component of 83329/POMTV& 50-32-8 0.000000 Not 1.0 N/A
56553/7PAH) Reported
Naphthalene (Component of 83329/POMTV) 91-20-3 8.67 8.86 1.0 -2.1%
Acetaldehyde 75-07-0 0.000030 Not 10.0 N/A
Reported
Acrolein 107-02-8 0.000040 Not 10.0 N/A
Reported
Ammonia(as NH3) 7664-41-7 7.32 Not 100.0 N/A
Reported
Benzene 71-43-2 386.77 395.09 1.0 -2.1%
Carbon disulfide 75-15-0 5.73 5.86 10.0 -2.1%
Chlorine 7782-50-5 173.38 177.11 100.0 -2.1%
DEHP(Di(2-ethylhexyl)phthalate) 117-81-7 266.74 272.48 10.0 -2.1%
Dibutylphthalate 84-74-2 18.67 19.07 100.0 -2.1%
Dichlorobenzene(p), 1,4- 106-46-7 6.40 6.54 1.0 -2.1%
Ethyl benzene 100-41-4 5.87 5.99 100.0 -2.1%
Ethyl chloride(chloroethane) 75-00-3 76.02 77.66 10.0 -2.1%
Fluorides (sum of all fluoride compounds as mass of F16984-48-8 1,107.97 1,008.17 10.0 9.9%
ion)
Formaldehyde 50-00-0 35.88 36.38 10.0 -1.4%
Hexane, n- 110-54-3 4.12 Not . 100.0 N/A
Reported
Hydrogen chloride (hydrochloric acid) 7647-01-0 1,510.73 1,498.63 100.0 0.8%
10/06/2015 Page 3 of 4

n
Facility Total CY 2014 Emission Summary Recorded in ED Facility ID #: 1900077
Facility Name: Triangle Brick Company-Merry Oaks Permit#(s): 06897T10
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants(TAPS) (Pounds/Year)
Pollutant CAS CY 2014 CY 2013 Demini- %
from ED from Fees mus Change
Hydrogen fluoride(hydrofluoric acid as mass of HF) 7664-39-3 693.15 630.79 100.0 9.9%
(Component of 16984488/Fluorides)
MEK(methyl ethyl ketone, 2-butanone) 78-93-3 29.34 29.97 100.0 -2.1%
Methyl chloride (chloromethane) 74-87-3 89.36 91.28 1.0 -2.1%
Methyl chloroform 71-55-6 0.626830 0.640320 100.0 -2.1%
Methyl iodide (iodomethane) 74-88-4 12.40 12.67 10.0 -2.1%
M1BK(methyl isobutyl ketone) 108-10-1 11.34 11.58 10.0 -2.1%
Perchloroethylene (tetrachloroethylene) 127-18-4 0.373430 0.381470 100.0 -2.1%
Phenol 108-95-2 11.47 11.72 100.0 -2.1%
Polycyclic Organic Matter(Inc PAH, dioxins, etc.NQom 0.011490 Not 1.0 N/A
&AP 42 historic) Reported
Selenium Compounds SEC 5.71 5.83 10.0 -2.1%
Styrene 100-42-5 2.67 2.72 100.0 -2.1%
Toluene 108-88-3 21.35 21.80 100.0 -2.1%
Xylene (mixed isomers) 1330-20-7 8.95 9.13 100:0 -1.9%
Xylene, o- 95-47-6 7.72 7.90 100.0 -2.3%
Largest Individual HAP Hydrogen chloride(hydrochloric acid) 1,510.73 lbs
Total HAP Emissions 3,414.32 lbs
DAQ's Comments Regarding Inventory
10/06/2015 Page 4 of 4

C' A
W1 Triangle Brick
6523 NC Highway 55
Durham, NC 27713
Durham:[phone]
Raleigh: [phone]
Toll Free:800-672-8547
Fax:[phone]
June 23,2015
North Carolina Department of
Environment and Natural Resources
Raleigh Regional Office
Air Quality Section
3800 Barrett Drive
Raleigh,North Carolina 27609
Attention: Air Emission Inventory
Reference: Submittal of 2014 Air Emission Inventory
Certification Form and Supporting Emission Calculations
Triangle Brick Company—Merry Oaks
Dear Sirs:
Enclosed please find the 2014 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 each 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. In addition, hydrogen fluoride, hydrogen chloride, and PM emissions are based on
site specific source testing. 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(919)544-1796 or Beth Barfield at(919)233-
4501.
Sincerely,
TRIANGLE BRICK COMPTL / A
Howard P.Brown, Jr.
Executive Vice President and Chief Operating Officer
cc: Ricky Merritt,Director of Engineering

2014 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.
1130 Situs Court, Suite 250
Raleigh, North Carolina 27606
June 2015

J
AERO EMISSION INVENTORY PRINTOUT
TRIANGLE BRICK COMPANY-MERRY OAKS

COPY of RECORD Date Submitted: 6/22/2015 10:05:45
I iventory Certification Form(Title V)
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 2014
These forms must be completed and returned even if the facility did not operate or emissions were zero
The legally defined "Responsible Official" of record for your facility is 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).
�ERTIFICATION STATEMENT:
'Important* Legally Responsible Official, i
certify that I am the responsible official for this facility,as described above, and hereby certify that the information contained
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 Sign d:
Printed Name: Howard Brown,Jr.
0-�,Sign : 26 -- 1
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: 6/22/2015 10:05:45 1

• COPY of RECORD Date Submitted: 6/22/2015 10:05:45
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 *CS ID *CS Description CD 1D'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]
CG-17 Feeders under Bins[NSPS 000]
CG-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]
CG-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]
CG-35 Belt to Screens [NSPS 000]
CG-36 Belt over Finish Screens [NSPS
000]
CG-37 Finish Screen[NSPS 000]
CG-38 IFinish 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 00.0]
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]
CG-49 Conveyor to Pug Mill [NSPS
000]
CG-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 000]
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
IS-6.2 sawdust screen
IS-7.1 conveyor to storage bin
IS-7.2 conveyor to storage bin
3

IS-8.1 oversize conveyor from sawdust
screen
IS-8.2 oversize conveyor from sawdust
screen
IS—CD-50 Conveyor from extruder to pug
mill
IS—CL1 Cosmetic loam operation area
IS—CL2 Cosmetic loam operation area
IS—EXTR1 Extrusion 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) [2D
1109 Case by Case MACT]
PC-1 Shale Feeder
PC-2 Scalp Screen[NSPS 000]
PC-3 Jaw Crusher[NSPS 000]
PC-4 Conveyor under PC-2 and PC-3
[NSPS 000]
4

a
PC-5 Cross over Conveyor[NSPS
000]
Shuttle Conveyor(Enclosed in
PC-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: 6/22/2015 10:05:45
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
ES Group ID ES 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
G-73 CG-32,CG-33,CG-34, �' 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-49,CG-46,CG-47,
CG-48,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 INONE
IS-CL1 NONE INONE
6

IS—CL2 NONE NONE
' IS—EXTRl NONE NONE
IS—EXTR2 NONE NONE
IS—LS 1 NONE NONE
IS—LS2 NONE NONE
21 No. 6 fuel oil tank—standing
IS—Tankl emissions
12 24,000 gallon No. 6 fuel oil storage
tank
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: 6/22/2015 10:05:45
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 2014
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 2014: 175484 TON/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) ro
Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry Hues):
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

Operating Scenario: OS— 15 Emission Source/Group ID: G-72
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
Hours 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 I 17% Farch—May 33% une—Aug. 33% ept.—Nov. 17%
014 4 �014 �014
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
2014
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)
2014
CO CO 08
NOx NOx 08
TSP TSP 5.18 08 0.059
PM10 PM10 5.18 08 0.059
PM2.5 PM2.5 5.18 08 0.059
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
2014
9

COPY of RECORD Date Submitted: 6/22/2015 10:05:45
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 2014
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-49,CG-46,CG-47,
CG-48,CG-5,CG-6,CG-7,CG-8,CG-9
2. Emission Source Description: Final Crushing and Grinding Operation
3. Operating Scenario ED/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 2014: 175484 TON/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) ro
Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS-ID CD ID Control Device Description
as listed 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= I 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 2014)
Hours 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:
Fan--Feb +Dec 15% Fach—May 35% une—Aug. 35% ept.—Nov. 15%
4 014 �014
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
2014
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po`�QS) Ef Control
Pollutants Code Pollutants Method Code (Net after Factor
(Tons/Year) (See Instructions) all controls)
2014
CO CO 08
NOz NOz 08
TSP TSP 2.19 08 0.025
PM10 PM10 0.2 08 0.0023
PM2.5 PM2.5 0.2 08 0.0023
S02 S02 08
VOC VOC 08
HAP/TAP Emissions Emission Control
CAS
Pollutants (In HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Factor
Alphabetical Order) (Pounds/Year) Method Code (Net after all controls)
See Instructions
2014
11

COPY of RECORD Date Submitted: 6/22/2015 10:05:45
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 2014
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 ED/Description: OS—21/No. 6 fuel oil tank—standing emissions
4. SCC Number/Description: Not required by facility,will be completed by DAQ
5. Throughput/units in 2014: 0.01 GAL/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter#): (F) (Feebsec) (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—21 Emission Source/Group ED:IS—Tankl
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% arch—May. 25% 014
25% Sept.—Nov. 25%
F014 014 014 014
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
2014
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)
2014
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 0 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
2014
13

COPY of RECORD Date Submitted: 6/22/2015 10:05:45
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 2014
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 2014:
(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-11) 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
14

Operating Scenario: OS— 12 Emission Source/Group ID: IS—Tankl
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% arch—May 25% 014
25% Sept.—Nov. 25%
2014 014 014 014
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
2014
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)
2014
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
2014
15

COPY of RECORD Date Submitted: 6/22/2015 10:05:45
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 2014
1. Emission Source ID(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: Not required by facility,will be completed by DAQ
5. Throughput/units in 2014: 1161 GAL/yr
(e.g.production or fuel use):
6. Fuel Information (if fuel is used) ro
Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
�--1 i i 1
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
FEP—FUG FUGITIVE(NO 1 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 2014)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu about:
ran--Feb +Dec 250�o arch—May 25% une—Aug. 25% ept.—Nov. 25%
4 014 014 014
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
2014
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(N�QS Code Pollutants Method Code (Net after Factor Ef Control
Pollutantss
(Tons/Year) (See Instructions) all controls)
2014
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 0„002 08
HAP/TAP Emissions Emission Control
Pollutants (in CAS HAP/TAPS Estimation EfficiencyEmission EF Control
Alphabetical Order) (Pounds/Year)
(see instructions) Method Code Factor
See Instructi (Net after all controls)ons
2014
17

COPY of RECORD Date Submitted: 6/22/2015 10:05:45
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 2014
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: Not required by facility,will be completed by DAQ
5. Throughput/units in 2014: 1161 GAL/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur ro
Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed in en-nit)
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
18

Operating Scenario: OS—23 Emission Source/Group ID:IS—Tank3
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
Fan—Feb +Dec 250�o arch—May 25"�u une—Aug. 250�o Sept.—Nov. 25%
0214 014 014 014
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
2014
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po�QS Code Pollutants Method Code (Net afterFactor Ef Control
Pollutantss
(Tons/Year) (See Instructions) all controls)
2014
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 0 08
HAP/TAP AP CAS Emissions Control
Pollutants (in FIAP/TAPS Estimation Efficient Emission EF Control
(see instructions) Method Code y Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2014
19

COPY of RECORD Date Submitted: 6/22/2015 10:05:45
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 2014
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 ED/Description: OS—24/No.2 fuel oil tank—standing and working emissions
4. SCC Number/Description: Not required by facility,will be completed by DAQ
5. Throughput/units in 2014: 1161 GAL/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) ro
Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—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
20

Operating Scenario: OS—24 Emission Source/Group ID: IS—Tank4
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 250�o arc ay 25% une—Aug. 25% 014
25%
2 114 014 014 014
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
2014
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)
2014
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 0 08
HAP/TAP CAS Emissions Emission Estimation Control Emission
Pollutants (In (see instructions) HAP/TAPS Efficiency Factor EF Control
Method Code
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2014
21

COPY of RECORD Date Submitted: 6/22/2015 10:05:45
As entered in AERO
Facility Name: Triangle Brick Company—Merry Oaks Facility ID : 1900077
294 King Rd Permit: 06897
Moncure,NC 27559 County : Chatham
DA-Q Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2014
1. Emission Source ID(from permit)or IS—Tanks
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 2014: 79425 GAL/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed in permit)
��71 i — i —
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) (Acfm)
Rectangle(L x W)
(in 0.1 feet)
EP—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 2014)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
ran--Feb +Dec 250�o arch—May 25"�o une—Aug. 25"�o Sept.—Nov. 2S'�„4 014 014 014
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
2014
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)
2014
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 0.3924 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
2014
23

COPY of RECORD Date Submitted: 6/22/2015 10:05:45
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 2014
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 2014: 9487 GAL/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur ro
Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point RP Information: Sources vented to more than one ERP use additional entry fines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
F
P—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 2014)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu about:
ran--Feb +Dec arch—May une—Aug. Sept.—Nov.
14 25% 014 25% 25%
4 2014
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
2014
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po�QS Code Pollutants Method Code Ef Control
Pollutantss (Net after Factor
(Tons/Year) (See Instructions) all controls)
2014
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC * '04- -0,21 08
HAP/TAP CAS Emissions Emission Estimation Control Emission
Pollutants (In HAP/TAPS Efficiency EF Control
(see instructions) Method Code
Alphabetical Order) (Pounds/Year) (Net after all controls) Factor
See Instructions
2014
��`h✓e��`1�1� `in ZOl f- was !L.4-�� h��ies �r, i:. ?_©/3 �o er»>'�s.i✓►-,5
25

COPY of RECORD Date Submitted: 6/22/2015 10:05:45
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 2014
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) [213 .1109 Case by C
3. Operating Scenario ID/Description: OS— l/Natural gas combustion—primary
4. SCC Number/Description: 30500335/Brick Manufacture—Curing Firing;Curing and Firing: Dual
Fuel—fired Kiln,Other Type
5. Throughputlunits in 2014: 2287000 FT3/yr
(e.g.production or fuel use):
6. Fuel Information (]f fuel is used) ro Sulfur /o 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 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)
lk-1 IVERTICAL STACKI 57.5 1 4 1 488 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 2014)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an-Feb +Dec 25% arch-May 25% une-Aug. 25% 014
25%
2014 014 014 014
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
2014
Emissions- Emission Control
Criteria Estimation
Pollutant Criteria Efficiency Emission
(NAAQS) Code Pollutants Method Code (Net after Factor Ef Control
Pollutants (See
(Tons/Year) all controls)
Instructions
2014
CO CO 0.1 08 0.000084
NOx NOx 0.11 08 0.0001
TSP TSP 0.01 08 0.0000076
PM10 PM10 0.01 08 0.0000076
PM2.5 PM2.5 0.01 08 0.0000076
S02 S02 0 08 6E-7
VOC VOC 0.01 08 0.0000055
Emissions Emission Control
HAP/TAP CAS Estimation Efficiency Emission
Alphabetical Order see instructions HAP/TAPS ll EF Control
Pollutants (In Al
p ) ( ) (Pounds/Year) Method Code (Net after all Factor
See Instructions controls)
2014
Acetaldehyde 75-07-0 0.00003 08 1.52E-11
Acrolein 107-02-8 0.00004 08 1.8E-11
Ammonia as NH3 7664-41-7 7.3184 08 0.0000032
Arsenic Unlisted Compounds( ASC-Other 0.00046 08 . 2E-10
Specify Component of ASC
Benzene 71-43-2 0.0048 08 2.1E-9
Benzo(a)pyrene(Component of 50-32-8 0 08 1.2E-12
POMTV POM7
Beryllium Compound,Unlisted BEC-Other 0.00003 08 1.2E-11
(Specify Component of BEC
Cadmium Metal(elemental
unreacted,Component of 7440-43-9 0.00252 08 1.1E-9
CDC
NSCR6-Other 0.0032 08 1.4E-9
27

Chromium(VI)Non—Specific,
knlisted(Specify Component
of NSCR6 CRC
Cobalt Unlisted Compound COC—Other 0.00019 08 8.4E-11
(Specify Component of COC
Hexane,n— 110-54-3 4.1166 08 0.0000018
Lead Unlisted Compounds
(Specify and Component of PBC—Other 0.00114 08 5E-10
PBC
Manganese Unlisted
Compounds (Specify MNC—Other 0.00087 08 3.8E-10
Component of MNC
Mercury,vapor(Component 7439-97-6 0.00059 08 2.6E-10
of HGC
Naphthalene(Component of 91-20-3 0.0014 08 6.1E-10
POMT
Nickel metal(Component of 7440-02-0 0.0048 08 2.1E-9
NIC
Selenium Compounds SEC 0.00005 08 2.4E-11
Toluene 108-88-3 0.00778 08 3.4E-9
28

COPY of RECORD Date Submitted: 6/22/2015 10:05:45
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 2014
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 I D/Description: OS—2/13istillate fuel and NG combustion—secondary
4. SCC Number/Description: 30500331Brick Manufacture—Curing Firing;-Curing and Firing: Dual Fuel
Fired Tunnel Kiln
5. Throughput/units in 2014:
(e.g.production or fael 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 DeN ice Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
lk-1 VERTICAL STACK 57.5 4 488 39.8 30008.49 ERP for Kiln 1
29

Operating Scenario: OS—2 Emission Source/Group ID:K-1
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
r01an--Feb +Dec 25% arch—May 25% une—Aug. 25% �014
ept.—Nov. 25%
4 014 �014
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
2014
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficienty Emission
Po� Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2014
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 Estimation Control Emission
Pollutants (In HAP/TAPS Efficiency EF Control
(see instructions) Method Code
Alphabetical Order) (Pounds/Year) (Net after all controls) Factor
See Instructions
2014
30

COPY of RECORD Date Submitted: 6/22/2015 10:05:45
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 2014
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: 30500331Brick Manufacture—Curing Firing;Curing and Firing: Dual Fuel
Fired Tunnel Kiln
5. Throughput/units in 2014:
(e.g.production or fuel use):
6. Fuel Information (if fuel is used) % Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
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)
lk-1 VERTICAL STACKI 57.5 4 1 488 T ,9.8 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 2014)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% 25% une—Aug. 25% �014
ept.—Nov. 25%
2 14 �arch—May-
14 014
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
2014
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)
2014
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 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
2014
32

COPY of RECORD Date Submitted: 6/22/2015 10:05:45
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 2014
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 ED/Description: OS—3/Natural gas combustion—primary
4. SCC Number/Description: 30500311Brick Manufacture—Curing Firing;Curing and Firing: Gas—fired
Tunnel Kilns
5. Throughputlunits in 2014:
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) ro
Sulfur /a 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)
1K-2 VERTICAL STACKI 57.5 4 1 488 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 2014)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 250�o 25% fne—Aug. 25% Sept.—Nov. 25%
2014 �arch—May
14 4 014
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
2014
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po�QS y Code Pollutants Method Code (Net after Factor Ef Control
Pollutantss
(Tons/Year) (See Instructions) all controls)
2014
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAPCAS Emissions Emission Estimation Control Emission
Pollutants (In HAP/TAPS Efficiency EF Control
(see instructions) Method Code
Alphabetical Order) (Pounds/Year) (Net after all controls) Factor
See Instructions
2014
34

COPY of RECORD Date Submitted: 6/22/2015 10:05:45
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 2014
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 ID/Description: OS—4/Distillate fuel and NG combustion—secondary
4. SCC Number/Description: 30500331/Brick Manufacture—Curing Firing;Curing and Firing: Dual Fuel
Fired Tunnel Kiln
5. Throughput/units in 2014:
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) r
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(Acfm)
Rectangle(L x W)
in 0.1 feet)
1K-2 VERTICAL STACK 57.5 4 488 39.8 J 30008.49 ERP for kiln 2
35

Operating Scenario: OS—4 Emission Source/Group ID:K-2
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year (�52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% 25"�o une—Aug. 25"�o Sept.—Nov. 25%
2014 �arch—May
14 014 014
13. Actual Emissions per Pollutant Listed c .I
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
2014
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)
2014
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 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
2014
36

COPY of RECORD Date Submitted: 6/22/2015 10:05:45
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 2014
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 ID/Description: OS— 18/Residual Oil and NG combustion—tertiary
4. SCC Number/Description: 30500331/Brick Manufacture—Curing Firing; Curing and Firing: Dual Fuel
Fired Tunnel Kiln
5. Throughput/units in 2014:
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) Sulfur ro
Ash Heat Content/o
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 in pennit)
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)
1K-2 VERTICAL STACK 57.5 4 488 39.8 30008.49 ERP for kiln 2
37

Operating Scenario: OS— 18 Emission Source/Groupj[D:K-2
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% 25% gJoune--Aug. 25% Sept.—Nov. 25%
014 �arch—IV[ay
14 14 014
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
2014
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)
2014
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 AP CAS Emissions Estimation Control Emission
Pollutants (In (see instructions) �P/TAPS Efficiency Factor EF Control
Method Code
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2014
38

COPY of RECORD Date Submitted: 6/22/2015 10:05:45
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 2014
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) [21) .1109 Case by Cas
3. Operating Scenario ED/Description: OS—5/NG combustion—primary
4. SCC Number/Description: 30500331Brick Manufacture—Curing Firing;Curing and Firing: Dual Fuel
Fired Tunnel Kiln
5. Throughputlunits in 2014: 133093 TON/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur ro
Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional en 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 IVERTICAL STACK 75 1 5 450 51 60082.95 ERP for Kiln 3
39

Operating Scenario: OS—5 Emission Source/Group ID:K-3
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% arch—May 25% une—Aug. 25% Sept.—Nov. 25%
2014 014 �014 014
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
2014
Emission
Criteria Emissions— Estimation Control
Pollutant Criteria Method' Efficiency Emission
(NAA Code Pollutants Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See all controls)
Instructions
2014
CO CO 38.4 08 0.577
NOx NOx 8.38 08 0.126
TSP TSP 25.08 08 0.3769
PM10 PM10 25.08 08 0.3769
PM2.5 PM2.5 25.08 08 0.3769
S02 S02 4.17 08 0.0627
VOC VOC 3.78 08 0.0568
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
2014
Antimony Unlisted Compounds(Specify SBC—Other 8.49133 08 0.0000638
Component of SBC
Arsenic Unlisted Compounds(Specify ASC—Other 3.04783 08 0.0000229
Component of ASC
Benzene 71-43-2 385.9697 08 0.0029
Beryllium metal(unreacted) 7440-41-7 0.0559 08 4.2E-7
(Component of BEC
Cadmium Metal(elemental unreacted, 7440-43-9 0.76662 08 0.00000576
Com onent of CDC
Carbon disulfide 75-15-0 5.723 08 0.000043
40

Chlorine 7782-50-5 173.0209 08 0.0013
Chromium Unlisted Compounds CRC-Other 2.78164 08 0.0000209
(Specify Component of CRC
Cobalt Unlisted Compound(Specify COC-Other 0.56831 08 0.00000427
Component of COC
Di 2-eth lhex 1 hthalate EHP) 117-81-7 266.186 08 0.002
Dibu 1 hthalate 84-74-2 18.63302 08 0.00014
Dichlorobenzene 14- 106-46-7 6.38846 08 0.000048
Eth l benzene 100-41-4 5.85609 08 0.000044
Ethyl chloride chloroethane 75-00-3 75.86301 08 0.00057
Fluorides(sum of all fluoride gs+.Ds O 00'1'
compounds) 16984-48-8 -5 . 08 .��
Formaldehyde 50-00-0 iT.-3;4-14 08 O.000 Z4v
Hydrogen chloride(hydrochloric acid 7647-01-0 08 4--tTO /
Hydrogen fluoride(hydrofluoric acid as G� 08 O.�3
mass of HF-Component of Fluorides 7664-39-3
Lead Unlisted Compounds(Specify and PBC-Other 19.96395 08 0.00015
Component of PBC
Manganese Unlisted Compounds MNC-Other 11.25967 08 0.0000846
(Specify Component of MNC
Mercury,vapor(Component of HGC 7439-97-6 1.33093 08 0.00001
Methyl chloride 74-87-3 89.17231 08 0.00067
Methyl.chloroform 71-55-6 0.62554 08 0.0000047
Methyl ethyl ketone 78-93-3 29.28046 08 0.00022
Methyl iodide 74-88-4 12.37765 08 0.000093
Methyl isobutyl.ketone 108-10-1 11.31291 08 0.000085
Naphthalene(Component of POM 91-20-3 8.65105 08 0.000065
Nickel metal(Component of NIC 7440-02-0 1.70359 08 0.0000128
Perchloroeth lene tetrachloroeth lene 127-18-4 0.37266 08 0.0000028
Phenol 108-95-2 11.446 08 0.000086
Selenium Compounds SEC 5.69638 08 0.0000428
Styrene 100-42-5 2.66186 08 0.00002
Toluene 108-88-3 21.29488 08 0.00016
X lene 1330-20-7 8.91723 08 0.000067
X lene o- 95-47-6 7.71939 08 0.000058
41

COPY of RECORD Date Submitted: 6/22/2015 10:05:45
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 2014
1. Emission Source ED(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) [213 .1109 Case by Cas
3. Operating Scenario W/Description: OS—6/Distillate and Natural gas combustion—secondary
4. SCC Number/Description: 30500312Brick Manufacture—Curing Firing; Curing and Firing: Oil—fired
Tunnel Kilns
5. Throughput/units in 2014: 275 TON/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur °/o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional 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)
1K-3 IVIERTICAL STACKI 75 5 450 51 60082.95 ERP for Kiln 3
42

n '
Operating Scenario: OS—6 Emission Source/Group ID:K-3
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 04 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an-Feb +Dec 250�o —May 250�o une—Aug. 25"�u �014
ept.—Nov. 25%
2 14 �arch
14 014
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
et after Factor Pollutants pollutants Code (N
(Tons/Year) (See all controls)
Instructions
2014
Emission
Criteria Emissions Estimation Control
Pollutant Criteria Method Efficiency
Emission
Po� Code Pollutants Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See all controls)
Instructions
2014
CO CO 0.09 08
NOx NOx 0.05 08
TSP TSP 0.06 08
PM10 PM10 0.05 08
PM2.5 PM2.5 0.05 08
S02 S02 0.13 08
VOC VOC 0.01 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
2014
Antimony Metal—add to SBC 7440-36-0 0.01753 08
Arsenic Metal,elemental unreacted
7440-38-2 0.00835 08
(Component of ASC
Benzene 71-43-2 0.79674 08
Beryllium metal(unreacted) 7440-41-7 0.00135 08
(Component of BEC
Cadmium Metal(elemental unreacted,
7440-43-9 0.00698 08
Component of CDC)
Carbon disulfide 75-15-0 0.01181 08
Chlorine 1 7782-50-5 1 0.35716 1 08
43

Chromium(VI)Non—Specific,Unlisted NSCR6—Other 0.00829 08
,(Specify Component of NSCR6 CRC
Chromium Unlisted Compounds CRC—Other 0.03399 08
(Specify Component of CRC
Cobalt Unlisted Compound(Specify
COC—Other 0.00117 08
Component of COC
Di 2—eth lhex 1 hthalate ERP) 117-81-7 0.54948 08
Dibu 1 hthalate 84-74-2 0.03846 08
Dichlorobenzene 1 4— 106-46-7 0.01319 08
Eth lbenzene 100-41-4 0.01209 08
Ethyl chloride chloroethane 75-00-3 0.1566 08
Fluorides (sum of all fluoride 16984-48-8 123.0826 08
compounds)
Formaldehyde 50-00-0 0.16718 08
Hydrogen chloride(hydrochloric acid 7647-01-0 46.70545 08
Hydrogen fluoride(hydrofluoric acid as
7664-39-3 76.92663 08
mass of HF—Component of Fluorides)
Lead Unlisted Compounds(Specify and
PBC—Other 0.04556 08
Component of PBC
Manganese Unlisted Compounds MNC—Other 0.0301 08
(Specify Component of MNC
Mercury,vapor(Component of HGC 7439-97-6 0.00422 08
Methyl chloride 74-87-3 0.18407 08
Methyl chloroform 71-55-6 0.00129 08
Methyl ethyl ketone 78-93-3 0.06044 08
Methyl iodide 74-88-4 0.02555 08
Methyl isobutyl ketone 108-10-1 0.02335 08
Naphthalene(Component of POMT 91-20-3 0.01786 08
Nickel metal(Component of NIC 7440-02-0 0.08711 08
Perchloroeth lene tetrachloroeth lene 127-18-4 0.00077 08
Phenol 108-95-2 0.02363 08
Polycyclic Organic Matter(Inc PAH,
dioxins,etc.NC AP 42 historic POM 0.01149 08
amorphous lob
Selenium Compounds SEC 0.01176 08
Styrene 100-42-5 0.00549 08
Toluene 108-88-3 0.04396 08
X lene 1330-20-7 0.03434 08
44

COPY of RECORD Date Submitted: 6/22/2015 10:05:45
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 : PRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2014
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 ED/Description: OS— 19/Residual Oil and NG combustion—tertiary
4. SCC Number/Description: 30500331Brick Manufacture—Curing Firing; Curing and Firing: Dual Fuel
Fired Tunnel Kiln
5. Throughput/units in 2014:
(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 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)
I K-3 IVERTICAL STACK 1 75 5 1 450 51 60082.95 ERP for Kiln 3
45

9
Operating Scenario: OS— 19 Emission Source/Group ID:K-3
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( `52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 250�o M 250�0. une—Aug. , 250�o �014
ept.—Nov. 25%
2014 �arch— ay
14 �014
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
2014
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
o� Code Pollutants Method Code (Net afterFactor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2014
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
Emission
HAP/TAP Emissions Control
CAS Estimation Emission
Pollutants (In (see instructions) BIAP/TAPS Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) See Instructions (Net after all controls)
2014
46

COPY of RECORD Date Submitted: 6/22/2015 10:05:45
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 2014
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 ED/Description: OS—20/Natural Gas Combustion
4. SCC Number/Description: 30500301Brick Manufacture—Dryer;Raw Material Drying
5. Throughput/units in 2014: 1184 TON/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur I 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 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
47

Operating Scenario: OS—20 Emission Source/Group ID: SD-1
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2014)
Hours 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 00 50% F014
e—Aug. 50% Sept.—Nov. 0%
2014 �arch—N.Iay
14 014
13. Actual Emissions per Pollutant Listed : o
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
(Tons ear) See Instructions all controls
2014
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po�QS Code Pollutants Method Code (Net afterFactor Ef Control
Pollutantss (Tons/Year) (See Instructions) all controls)
2014
CO CO 0 09
NOx NOx 0 09
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 0 09
VOC VOC 0 09
HAP/TAP Emissions
Emission Control
CAS Estimation Efficient Emission
Pollutants (In see instructions HAP/TAPS y EF Control
( )
Alphabetical Order) (Pounds/Year) Method Code (Net after all Factor
See Instructions controls)
2014
Formaldehyde 50-00-0 0 09
48

Facility Total CY 2014 Emissions Summary {
COPY of RECORD Date Submitted: 6/22/2015 10:05:45
As entered in AERO
Facility Name: Triangle Brick Company—Merry Oaks j 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 2014
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 2014 2013 % Change
Criteria Pollutants
Actual Emissions Tons/Year
Pollutant CAS 2014 2013 % Change
CO CO 38.59 39.31 —1.831598%
NOx NOx 8.54 8.6 —0.6976793%
PM TSP TSP 32.53 32.06 1.465993%
PM 10 PM 10 30.53 24.58 24.206675%
PM2.5 PM2.5 30.53 24.5.8 24.206675%
S02 I S02 4.3 4.27 0.70258105%
VOC I VOC 4.36 4.66 —6.4377623%
Hazardous Air Pollutants HAPS and/or Toxic Air Pollutants TAPS
Actual Emissions Pounds/Year
Pollutant I CAS 1 2014 2013 % Change
Pollutant Grou :Antimon Compounds total mass, me elemental SB Group Sum:8.50886
Antimony Metal—add to SBC 7440-36-0 0.01753 Not reported N/A
Antimony Unlisted Compounds(Specify SBC—Other 8.49133 8.69205 —2.3092346%
Component of SBC
Pollutant Group:Arsenic Compounds(total mass of elemental AS, arsine and all inorganic compounds) Group
Sum:3.05664
Arsenic Metal,elemental unreacted 7440-38-2 0.00835 Not reported N/A
(Component of ASC
Arsenic Unlisted Compounds( Specify ASC—Other 3.04829 3.11987 —2.2943242%
Component of ASC
Pollutant Group:Beryllium compounds Total mass Group Sum:.05728
Beryllium Compound,Unlisted(Specify
BEC—Other 3.0E-5 Not reported N/A
Component of BEC
Beryllium metal(unreacted)(Component 7440-41-7 0.05725 .05722 0.052428804%
of BEC
49

Pollutant Grou :Cadmium compounds total mass inc elemental metal Group Sum:.77612
:Cadmium Metal(elemental unreacted, 7440-43-9 0.77612 .78474 -1.0984485%
Component of CDC
Pollutant Grou :Chromium VI Non-Specific Compounds,as Chrom VI (Component CRC Grou Sum*
.01149
Chromium(VI)Non-Specific,Unlisted NSCR6-Other 0.01149 Not reported N/A
(Specify Component of NSCR6 CRC
Pollutant Group:Chromium-All/Total Inc Chromium I cate ories,metal and Others Group Sum:2.82712
Chromium(VI)Non-Specific,Unlisted NSCR6-Other 0.01149 Not reported N/A
(Specify Component of NSCR6 CRC
Chromium Unlisted Compounds(Specify CRC-Other 2.81563 2.8474 -1.1157544%
Component of CRC
Pollutant Grou :Cobalt compands Grou Sum:.56967
Cobalt Unlisted Compound(Specify COC-Other 0.56967 .58174 -2.07481%
Component of COC
Pollutant Grou :Lead and Lead compounds Group Sum:20.01065
Lead Unlisted Compounds
Com onent of PBC(Specify and PBC-Other -F 20.01065 20.43585 -2.0806549%
Pollutant Grou :Man anese compounds Grou Sum:11.29064
Manganese Unlisted Compounds(Specify MNC-Other 11.29064 11.52582 -2.0404613%
Component of MNC
ollutant Group:Mercury Compounds-all total mass,inc Hg Vapor Group Sum:1.33574
Mercury,vapor Com onent of HGC 1 7439-97-6 1 1.33574 1 1.36239 -1.9561263%
Pollutant Grou :Nickel Compounds, sum total mass,inc elemental Group Sum:1.7955
Nickel metal(Component of NIC 7440-02-0 1.7955 1 1.74386 2.9612489%
Pollutant Grou :Pol c clic Organic Matter 7 PAH Compound for NIF Group Sum:0
Benzo(a)pyrene(Component of POMTV POM7) 50-32-8 0.0 Not reported N/A
ollutant Grou :Pol c clic Organic Matter(Specific Com ounds from OA PS for TV Group Sum:8.67031
Benzo(a)pyrene(Component of POMTV 50-32-8 0.0 Not reported N/A
POM7
Naphthalene(Component of POMTV 91-20-3 8.67031 8.85554 -2.0916877%
Acetaldehyde 75-07-0 3.0E-5 Not reported N/A
Acrolein 107-02-8 4.0E-5 Not reported N/A
Ammonia as NH3 7664-41-7 7.3184 Not reported N/A
Benzene 71-43-2 386.77124 395.0931 -2.1063058%
Carbon disulfide 75-15-0 5.73481 5.85828 -2.1076205%
Chlorine 7782-50-5 173.37807 177.1107 -2.1075156%
Di 2-eth lhex 1 hthalate DEHP 117-81-7 266.73547 272.478 -2.1075182%
Dibu 1 hthalate 84-74-2 18.67148 19.07346 -2.107533%
Dichlorobenzene , 1,4- 106-46-7 6.40165 6.53947 -2.107514%
Ethyl benzene 100-41-4 5.86818 5.99452 -2.107598%
Ethyl chloride chloroethane 75-00-3 76.01961 77.65623 -2.1075187%
Fluorides sum of all fluoride compounds) 16984-48-8 59748.746 1008.1686 5826.464%
Formaldehyde 50-00-0 17.50135 36.38069 -51.89385%
Hexane n- 110-54-3 4.1166 Not reported N/A
Hydrogen chloride(hydrochloric acid 7647-01-0 22672.516 1498.629 1412.8838%
Hydrogen fluoride(hydrofluoric acid as 7664-39-3 37342.965 630.78657 5820.064%
mass of HF-Component of Fluorides
Methyl chloride 74-87-3 89.35638 91.28013 -2.1075253%
Methyl chloroform 71-55-6 0.62683 .64032 -2.1067624%
50

Methyl ethyl ketone 78-93-3 29.3409 29.97258 —2.1075246%
Methyl iodide 74-88-4 12.4032 12.67023 —2.1075368%
Methyl isobutyl ketone 108-10-1 11.33626 11.58032 —2.1075454%
Perchlordeth lene tetrachloroeth lene 127-18-4 0.37343 .38147 —2.1076314%
Phenol 108-95-2 11.46963 11.71655 —2.107443%
Polycyclic Organic Matter(Inc PAH,
dioxins,etc.NC AP 42 historic amorphous POM 0.01149 Not reported N/A
lob
Selenium Compounds SEC 5.70819 5.83103 —2.1066592%
Styrene 100-42-5 2.66735 2.72478 —2.1076941%
Toluene 108-88-3 21.34662 21.79824 —2.071819%
X lene 1330-20-7 8.95157 9.12801 —1.9329541%
X lene,o— 95-47-6 7.71939 7.90186 —2.3092072%
51

COPY of RECORD Date Submitted: 6/22/2015 10:05:45
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:
6/19/2015—Operating Scenario Comments
OS OS5 :Uncontrolled emission factor for Hydrogen Fluoride and Hydrogen Chloride based on source test completed August
2006.DLA was operated a few days each month to maintain it,but the associated reduction is not accounted for in these
calculations.
6/19/2015—Operating Scenario Comments
OS OS6 : Uncontrolled emission factor for Hydrogen Fluoride and Hydrogen Chloride based on source test completed August
2006. DLA was operated a few days each month to maintain it,but the associated reduction is not accounted for in these
calculations.
6/19/2015—Operating Scenario Comments
OS OS21 : Standing emissions only.No throughput for the reporting year. (Entered 0.01 for the throughput because AERO
does not allow inputs of 0 throughput.)
6/12/2015—Operating Scenario Comments
OS OS13 : VOC emissions are working and breathing losses OS OS13
6/12/2015—Operating Scenario Comments
OS OS 14 : VOC emissions are working and breathing losses
52

I�
SUPPORTING EMISSION CALCULATIONS
TRIANGLE BRICK COMPANY-MERRY OAKS

Table A-1
Calculation of Actual 2014 Air Emissions From Brick Tunnel Kiln#1
(Source I.D.-K-1)
Triangle Brick Company
Merry Oaks,North Carolina
Production Data
Tons of Fired Brick Produced I 0 tons
Cubic Feet Natural Gas Combusted 1 2287 000
Gallons Distillate Oil 2-1-led0 .lions
Gallons Residual Oil Combusted 0 .Ions
Tons Brick Fired With Natural Gas 0 tons
Tons Brick Fired With Distillate Oil I 0 tons
Tons Brick Fired With Residual Oil I 0 tons
Primary Operating Scenario S...ndary Operating Scenario Tertiary Operating Scenario Emissions Summary
NC TAP 8/or Cla Firin Natural Gas ClayFiringDistillate 011 Distillate Fuel Combustion Total ClayFiringResidual Oil Residual Fuel Combustion Total
Pollutant CAS Number HAP Emission 1 Actual Emission Actual Emission Actual O er.Scan. Emission Actual Emission Actual O er.Scan. Total 2014 Total 2014
Factor Emission Rate Factor Emission Rate Factor Emission Rate Emissions Factor Emission Rate Factor Emission Rate Emissions Emissions Emissions
Ibstton (Ib Ibsttan Ib. r (tu/1000gallon) Ibs/yr) (Ib r) (ibs7ton) (Ibs r (I1,/1 D00gallon) (ib ) (Ibe r) (lb.) (tons)
TSP° Neither 0.13 0.00 0.13 0.00 2.0 0.00 0.00 0.13 0.00 2205 0,00 0.00 0.00 0.00
PM-10° Neither 0.13 0.00 0.13 0.00 1.1 0.00 0.00 0.13 0.00 19.6 0.00 0.00 0.00 0.00
PM-2.5 Neither 0.13 0.00 0.13 0.00 1.1 0.00 0.00 0.13 0.00 1946 0.00 0.00 0.00 0.00
S02 Neither 0.0627 0.00 0.0627 0.00 71.0 0.00 0.00 0,0627 0.00 329.7 0.00 0.00 0.00 0.00
NO. Neither 0.126 0.00 0.126 0.00 20.0 0.00 0.00 0.126 0.00 1 55.0 0.00 0.00 0.00 0.00
Co Neither 0.577 0.00 0.577 0.00 5.0 0.00 0.00 0.577 0.00 5.0 0.01) 0.00 0.00 0.00
VOC Neither 0.0568 0.00 0.0568 0.00 0.2 0.00 0.00 0.0568 0.00 0.3 0.00 0.00 0.00 0.00
1,1,1 Trichloroethane 71-55-6 TAP/HAP 4.70E-06 0.00 4.70E-06 0,00 N/A 0.00 0.00 4.70E-06 0.00 N/A 0.00 0.00 0.00 0.00
1A Dichlorobenzene 106-46-7 TAP/HAP 4.80E-05 0.00 4.80E-05 0.00 N/A 0.00 0.00 4.80E-05 0.00 N/A 0.00 0.00 0.00 0.00
2-Butanone MEK 78-93-3 TAP/HAP 2.20E-04 0.00 2.20E-04 0.00 N/A 0.00 0.00 2.20E-04 0.00 NIA 0.00 0.00 0.00 0.00
2-Hexan me MIRK 59148-6 TAP/HAP 8.50E-05 0.00 8.50E-05 0.00 N/A 0.00 0.00 8.50E-05 0.00 NIA 0.00 0.00 0.00 0.00
Acetone 67-04-1 Neither 1.70E-03 0.00 1.70E-03 0.00 N/A 0.00 0.00 1.70E-03 0.00 NIA 0.00 0.00 0.00 0.00
An6mon :.9Gmer O HAP 6.38E-05 0.00 6.78E-05 0.00 NIA 0.00 0.00 6.38E-05 0.00 5.25E-03 0.00 0.00 0.00 0.00
Arsenic ASC Other TAP/HAP 2.29E-05 0.00 2.29E-05 0.00 5.92E-04 0.00 0.00 2.29E-05 0.00 1.32E-03 0.00 0.00 0.00 0.00
Benzene 71-43-2 TAP/HAP 2.90E-03 0.00 2.90E-03 0.00 N/A 0.00 0.00 2.90E-03 0.00 2.14E-04 0.00 0.00 0.00 0.00
Benzo a rene POM PO4 TAP N/A 0.00 N/A 0.00 3.30E-03 0.00 0.00 N/A 0.00 1.20E-03 0.00 0.00 0.00 0.00
Be Ilium 7440-41-7 TAP/HAP 4.27E-07 0.00 4.27E-07 0.00 3.53E-04 0.00 0.00 4.27E-07 0.00 2.78E-05 0.00 0.00 0.00 0.00
Bis 2-eth Ihex Phthalate 117-81-7 HAP 2.00E-03 0.00 2.00E-03 0.00 NIA 0.00 0.00 2.00E-03 0.00 N/A 0.00 0.00 0.00 0.00
Bu Iben I hthalate 85-68-7 Neither 1.80E-05 0.00 1.80E-05 0.00 N/A 0.00 0.00 1.80E-05 0.00 NIA 0.00 0.00 0.00 0.00
Cadmium 7440-43-9 TAP/HAP 5.76E-06 0.00 5.76E-06 0.00 1.55E-03 0.00 0.00 5.76E-06 0.00 3.98E-04 0.00 0.00 0.00 0.00
Carbon Disulfide 1 75-15-0 1 TAP/HAP 4.30E-05 0.00 4.30E-05 0.00 N/A 0.00 O.oD 4.30E-05 0.00 N/A 0.00 0.00 0.00 0.00
Chlorine 7782-50-5 1 TAP/HAP 1.30E-03 0.00 1.30E-03 0.00 NIA 0.00 0.00 1.30E-03 0.00 NIA 0.00 0.00 0.00 0.00
Chloroethane 75-00-J HAP 5.70E-04 0.00 5.70E-04 0.00 N/A 0.00 0.00 5.70E-04 0.00 N/A 0.00 0.00 0.00 0.00
Chloromethane 74-87-J HAP 6.70E-04 0.00 6.7DE-04 0.00 N/A 0.00 0.00 6.70E-04 0.00 N/A 0.00 0.00 0.00 0.00
Chrome VI PSCR6-Othm TAP/HAP N/A 0.00 NIA 0.00 2.38E-03 0.00 0.00 N/A 0.00 2.48E-04 0.00 0.00 0.00 0.00
Chromium CRC-Other HAP 2.09E-05 0.00 2.09E-OS 0.00 8.11E-03 0.00 0.00 2.09E-OS 0.00 8.45E-04 0.00 0.00 0.00 0.00
1 of 2

Table A-1
Calculation of Actual 2014 Air Emissions From Brick Tunnel Kiln#1
(Source I.D.-K-1)
Triangle Brick Company
Merry Oaks,North Carolina
Production Data
Tons of Fired Brick Produced I 0 tons
Cubic Feet Natural Gas Combusted 2287000
Gallons Distillate Oil Combusted 0 allons
Gallons Residual Oil Combusted 0 .Ions
Tons Brick Fired With Natural Gas 0 tons
Tons Brick Fired With Distillate Oil 0 tons
Tons Brick Fired With Residual Oil 0 tans
Primary Operating Scenario Secondsry Operating Scenario Tertiary Operating Scenario Emissions Summary
NC TAP 8/or Clamisio Firin Natural Gas ClayFiringDistillate Oil Distillate Fuel Combustion Total ClayFiringResidual 01I Residual Fuel Combustion Total
Pollutant CAS Number HAP Esn Actual Emission Actual Emission Actual O er.Scan. Emission Actual Emission Actual Op"
Seen. Total 2014 Total 2014
Factor Emission Rate Factor Emission Rate Factor Emission Rate Emissions Factor Emission Rate Factor Emission Rate Emissions Emissions Emissions
(Ibs/ton) (lb,,) (lbsthm) (Ibs/yr) (11,11000 gallon) (lbs/yr) Ib r Ibstton) (Ibs/r y) (16/1000gallon) Qbs ) Ibs r (lb,) (tons)
Cobalt COC-Other HAP 4.27E-06 0.00 4.27E-06 0.00 N/A 0.00 0.00 4.27E-06 0.00 6.02E-03 0.00 0.00 0.00 0.00
Di Butyl Phthalate 84-74.2 HAP 1.40E-04 0.00 1.40E-04 0.00 WA 0.00 0.00 1.40E-04 0.00 WA 0.00 0.00 0.00 0.00
Dieth hthalate 84-66.2 Neither 2.40E-04 0.00 2.40E-04 0.00 WA 0.00 0.00 2.40E-04 0.00 WA 0.00 0.00 0.00 0.00
EthylBenzene 100414 HAP 4.40E-05 0.00 4.40E-05 0.00 WA 0.00 0.00 4.40E-05 0.00 6.36E-05 0.00 0.00 0.00 0.00
Formaldeh de 50-00-0 TAP/HAP WA 0.00 WA 0.00 4.80E-02 0.00 0.00 WA 0.00 425E-02 0.00 0.00 0.00 0.00
Hydrogen
Chloride 7647-01-0 TAP/HAP 1.70E-01 0.00 1.70E-01 0.00 WA 0.00 0.00 1.70E-01 0.00 WA 0.00 0.00 No 0.00
Hydrogen Fluoride 7664-39-3 TAP/HAP 2.80E-01 0.00 2.80E-01 0.00 WA 0.00 0.00 2.80E-01 0.00 WA 0.00 0.00 0.00 0.00
lodomethane 74-884 HAP 9.30E-05 0.00 9.30E-05 0.00 N/A 0.00 0.00 9.30E-05 0.00 WA 0.00 0.00 0.00 0.00
Lead PSC-Other' HAP 1.50E-04 0.00 1.50E-04 0.00 125E-03 0.00 0.00 1.50E-04 0.00 1.51E-03 0.00 0.00 0.00 0.00
Manganese MNC-Other TAP/HAP 8.46E-05 0.00 8.46E-05 0.00 1.97E-03 0.00 0.00 8.46E-05 0.00 3.00E-03 0.00 0.00 0.00 0.00
Mercury' 7439-976 TAP/HAP 1.00E-05 0.00 1.00E-05 DAG 423E-04 0.00 o.0o 1.00E-05 0.00 1.13E-04 0.00 0.00 0.00 0.00
Na hthalene' 91-20-3 HAP 6.50E-05 0.00 6.50E-05 0.00 WA 0.00 0.00 6.50E-05 0.00 1.13E-03 0.D0 0.00 0,00 0.00
Nickel- 7440-02-0 TAP/HAP 1.28E-05 0.00 128E-05 0.00 2.40E-02 0.00 0.00 128E-05 0.00 8.45E-02 0.00 0.00 0.00 0.00
Phenol 108-95-2 TAP/HAP 8.60E-05 0.00 8.60E-05 0.00 WA 0.00 0.00 8.60E-05 0.00 WA 0.00 0.00 0.00 0.00
Selenium' SEC HAP 4.28E-05 020 4.28E-05 0.00 WA 0.00 0.00 4.28E-05 0.00 6.83E-04 0.00 0.00 0.00 0.00
Styr.na2 10042-5 TAP/HAP 2.00E-05 0.00 2.00E-05 0.00 WA 0.00 0.00 2.00E-05 0.00�NtA
0.00 0.00 0.00 0.00
Tetrachloroet7 127-184 TAP/HAP 2.80E-06 0.00 2.80E-06 0.00 WA 0.00 0.00 2.80E-06 0.000.00 0.00 0.00 0.00
Toluene 108-08-3 TAP/HAP 1.60E-04 0.00 1.60E-04 0.00 WA 0.00 0.00 1.60E-04 0.00 0.00 0.00 0.00 0.00
Total Fluorides 169844641 TAP 4.48E-01 0.00 4.48E-01 0.00 WA 0.00 0.00 4.48E-01 0.00 0.00 0.00E.00 0.00 0.00
Xylene 1330-20-7 TAP/HAP 1.25E-04 0.00 125E-04 0.00 N/A 0.00 0.00 1.25E-04 0.00 1.09E-01 0.00 0.00 0.00 0.00
1. Emission factor based on USEPA/Brick Association of North Carolina sponsored source test completed at Triangle Brick Company's Merry Oaks,North Carolina facility.
1a.Emission factor for TSP based on Stack Test dated August 2006.PM-10 set equal to TSP due to AERO limitation.
2. Emission factors obtained from AP42 Section 11.3"Brick and Structural Clay Products",Final report,August 1997.
3. Uncontrolled emission factor for Hydrogen Fluoride and Hydrogen Chloride based on source test completed August 2006.DLA was operated a few days each month to maintain it,but the associated reduction is not accounted for in these calculations.
4. Fuel combustion emission factors obtained from AP42 Section 1.3"Fuel Oil Combustion"and NCDEM guidance. -
5. Heat input rating assumed to be 140,000 Btu/gallon for No.2 fuel oil and 150,000 Btu/gal for No.6 fuel oil.
6. Sulfur content of No.2 fuel oil assumed to be 0.51.
7. Sulfur content of No.6 fuel oil assumed to be 2A%.
8. Emission factor for Total Fluorides is(1.6)x(Hydrogen Fluoride emission factor).
2 of

Table A-2
Calculation of Actual 2014 Air Emissions From Brick Tunnel Kiln k2
(Source I.D.-K-2)
Triangle Brick Company
Merry Oaks,North Carolina
Production Data
Tons of Fired Brick Produced 0 tons
Cubic Feet Natural Gas Combusted 0 it
Gallons Distillate Oil Combusted 0 allons
Gallons Residual Oil Combusted 0 g.11ons
Tons Brick Fired Wth Natural Gas 0 tons
Tons Brick Fired With Distillate Oil 0 tons
Tons Brick Fired VVdh Residual Oil 1 0 tons
Primary Operafing Scenario Secondary O era0n Scenario Tertiary Operating Scenario Emissions Summary
NC TAP&/or Cie Firin Nat.Gas ClayFidn Nat.Gas Distillate Fuel Combustion Total ClayFiringNat.Gas Residual Fuel Combustion" Total
Pollutant CAS Number HAP Emission I Actual Emission Actual Emission Actual O er.Scen. Emission Actual Emission Actual O er.Scen. Total 2014 Total 2014
Factor Emission Rate Factor Emission Rate Factor Emission Rate Emissions Factor Emission Rate Factor Emission Rate Emissions Emissions Emissions
ohm s r n s r / O a on s q anon sl r b/ O a on s r s r (lbs) ((tons)
TSP Neither 0.13 0.00 0.13 0.00 2.0 0.00 0.00 0.13 0.00 22.5 0.00 0.00 0.00 0.00
PM-10' Neither 0.13 0.00 D.13 0.00 1.1 0.00 D.00 0.13 0.00 19S 0.00 0.00 0.00 0.00
PM-2.5 Neither 0.13 0.00 0.13 0.00 1.1 0.00 O.Oo 0.13 0.00 19.6 0.00 0.00 D.OD 0.00
S02 Neither 0.0627 0.00 0.0627 0.00 71.0 0.00 0.00 0.0627 0.00 329.7 0.00 0.00 0.00 0.00
NO.' Neither 0.126 0.00 0.126 0.00 20.0 0.00 0.00 0.126 0.00 55.0 0.00 0.00 0.00 0.00
CO Neither 0.577 0.00 0.577 0.00 5.0 0.00 0.00 0.577 0.00 1 5.0 0.00 0.00 0.00 0.00
VOC Neither 0.0568 0.00 0.0568 0.00 0.2 0.00 0.00 0.0568 0.00 0.3 0.00 0.00 0.00 0.00
1,11 Trichioroethane 71-55-6 TAP/HAP 4.70E-06 0.00 4.70E-06 0.00 NIA 0.00 0.00 4.70E-06 0.00 N/A 0.00 0.00E+00 0.00 0.00
4 1, Dichlorobenzene 106-46-7 TAP/HAP 4.80E-05 0.00 4.80E-05 0.00 N/A 0.00 0.00 4.80E-05 0.00 NIA 0.00 0.00E+00 0.00 0.00
2-Butanone MEK 78-93-3 TAP/HAP 220E-04 0.00 2.20E-04 0.00 N/A 0.00 0.00 2.20E-04 0.00 N/A 0.00 0.00E+00 0.00 0.00
2-Hexanone MIRK 591-7M TAP/HAP 8.50E-05 0.00 8.50E-05 ciao N/A 0.00 0.00 8.50E-05 0.00 N/A 0.00 O.00E+00 O.OD O.DO
Acetone 67-04-1 Neither 1.70E-03 0.00 1.70E-03 0.00 N/A 0.00 0.00 1.70E-03 0.00 N/A 0.00 O.00E+00 0.o0 0.00
Antimon ssc-Other HAP 6.38E-05 0.00 6.38E-05 0.00 N/A 0.00 0.00 6.38E-05 0.00 5.25E-03 0.00 0.00E+00 0.00 0.00
Arsenic CSC-Other TAP/HAP 2.29E-05 0.00 2.29E-05 0.00 5.92E-04 0.00 0.00 2.29E-05 0.00 1.32E-03 0.00 0.00E+00 0.00 0.00
Benzene 71-43-2 TAP/HAP 2.90E-03 0.00 2.90E-03 0.00 N/A 0.00 0.00 2.90E-03 0.00 2.14E-04 0.00 O.00E+00 0.00 0.00
Be a rene POM POM TAP N/A 0.00 NIA 0.00 3.30E-03 0.00 0.00 N/A 0.00 1.20E-03 0.00 O.00E+00 0.00 0.00
Be Ilium 744--41-7 TAP/HAP 4.27E-07 0.00 4.27E-07 0.00 3.53E-04 0.00 0.00 4.27E-07 0.00 2.78E-05 0.00 0.00E+00 0.00 0.00
Bis 2-eth Ihex Phthalate 117-81-7 HAP 2.00E-03 0.00 2.00E-03 0.00 N/A 0.00 0.00 2.00E-03 0.00 N/A 0.00 0.00E+00 0.00 0.00
Bu Iben I hthalate 85-68-7 Neither 1.80E-05 0.00 1.80E-05 ciao N/A 0.00 0.00 1.80E-05 0.00 N/A 0.00 O.00E+00 0.00 0.00
Cadmium 7440-43-9 TAP/HAP 5.76E-06 0.00 5.76E-06 0.00 1.55E-03 0.00 O.00 5.76E-06 0.00 3.98E-04 0.00 0.00E+00 0.00 0.00
Carbon Disulfide 75-15-0 TAP/HAP 4.10E-05 0.00 4.30E-05 0.00 N/A 0.00 0.00 4.30E-05 0.00 N/A 0.00 0.00E+00 0.00 O.DO
Chlorine 7782-50-5 TAP/HAP 1.30E-03 0.00 1.30E-03 0.00 NIA 0.00 D.Oo 1.30E-03 0.00 N/A 0.00 0.00E+00 0.00 0.00
Chloroethane 75-01-3 HAP 5.70E-04 0.00 5.70E-04 0.00 NIA 0.00 0.00 5.70E-04 0.00 N/A 0.00 0.00E+00 0.00 O.OII
Chl-methane 74-87-3 HAP 6.70E-04 0.00 6.70E-04 O.OD N/A 0.00 0.00 6.70E-04 0.00 N/A 0.00 0.00E+00 0.00 0.00
Chrome Vl NSCR6-011- TAP/HAP N/A 0.00 N/A 0.00 2.38E-03 0.00 0.00 N/A 0.00 2.48E-04 0.00 0.0DE+00 0.00 0.00
Chromium CRG-Ot1i:i HAP 2.09E-05 0.00 2.09E-OS 0.00 8.11E-03 0.00 0.00 2.09E-OS 0.00 8.45E-04 0.00 0.00E+00 0.00 c.00
1 of 2

Table A-2
Calculation of Actual 2014 Air Emissions From Brick Tunnel Kiln#2
(Source I.D.-K-2)
Triangle Brick Company
Merry Oaks,North Carolina
Production Data
Tons of Fired Brick Produceddallon:s
Cubic Feet Natural Gas Combusted
Gallons Distillate Oil CombustedGallons Residual Oil CombustedTons Brick Fired With Natural GasTons Brick Fired WM Distillate OilTons Brick Fired With Residual Oil
"'in.,
rima Ciperafing Scenario Seconds O"ratio Scenario TertiaryOperating Scenario missions Summary
NC TAP Wor Cla FiringNat.Gas ClayFiringNat.Gas Distillate Fuel Combustion Total Cla Firin Nat.Gas Residual Fuel Combustion Total
Pollutant CAS Number HAP Emission Actual Emission Actual Emission Actual O er.Scen. Emission Actual Emission Actual O er.Seen. Total 2014 Total 2014
Factor Emission Rate Factor Emission Rate Factor Emission Rate Emissions Factor Emission Rate Factor Emission Rate Emissions Emissions Emissions
(Ibs/ton (bsfyr) ( ston bs r @/1000 allon) (Ibs/yr) bs/ton) 1 s/r (Ib/000 a an) (Ibs s r ( s tons)
Cobalt C040thc, HAP 4.27E-06 0.00 4.27E-06 0.00 N/A 0.00 0.00 4.27E-06 0.00 6.02E-03 0.00 0.00E+00 O.ou 0.00
Di Butyl Phthalate 84-74-2 HAP 1.40E-04 0.00 1.40E-04 0.00 WA 0.00 0.00 1.40E-04 0.00 WA 0.00 0.00E+00 0.00 0.00
Dieth 1 hthalate 84-W2 Neither 2.40E-04 0.00 2.40E-04 0.00 WA 0.00 0.00 2.40E-04 0.00 WA 0.00 O.oOE+00 0.00 0.00
Ethyl Benzene 100414 HAP 4.40E-05 0.00 4,40E-05 0.00 WA 0.00 0.00 4.40E-05 0.00 6.36E-05 0.00 0.00E+00 0.00 0.00
Formaldeh de 50-00-0 TAP/HAP WA 0.00 WA 0.00 4.80E-02 0.00 0.00 WA 0.00 4.25E-02 0.00 0.00E+00 0.00 0.00
H dro en Chloride 7647-014 TAP/HAP 1.70E-01 0.00 1.70E-01 0.00 WA 0.00 0.00 1.70E-01 0.00 WA N.0.0
0.00E+00 0.00 0.00
Hydrogen Fluoride 7664-39-3 TAP/HAP 2.80E-01 0.00 2.80E-01 0.00 WA 0.00 0.00 2.80E-01 0.00 WA O.00E+00 0.00 0.00
lodomethane 744" HAP 9.30E-05 0.00 9.30E-05 0.00 WA 0.00 0.00 9.30E-05 0.00 WA 0.00E+00 0.00 0.00
Lead PSC-Other' HAP 1.50E-04 0.00 1.50E-04 0.00 125E-03 0.00 0.00 1.50E-04 0.00 1.51E-030.00E+00 0.00 0.00
Manganese' MNC-Other TAP/HAP 8.46E-05 0.00 8.46E-05 0.00 1.97E-03 0.00 0.00 8.46E-05 0.00 3.00E-03O.00E+00 0.00 0.00
Mercury7439-97-0 TAP/HAP 1.00E-05 0.00 1.00E-05 0.00 423E-04 0.00 0.00 1.00E-05 0.00 1.13E-040.00E+00 0.00 0.00
Naphthalene' 91-20-3 HAP 6.50E-05 0.00 6.50E-05 0.00 WA 0.00 0.00 6.50E-05 0.00 1.13E-030.00E+00 0.00 0.00
Nickel 7440-02-0 TAP/HAP 1.28E-05 0.00 1.28E-05 0.00 2.40E-02 0.00 0.00 128E-05 0.00 8.45E-02O.00E+00 0.00 0.00
Phenol 108-05-2 TAP/HAP 8.60E-05 0.00 8.60E-05 0.00 WA 0.00 0.00 8.60E-05 0.00 WA 0.00E+00 0.00 0.00
Selenium SEC HAP 4.28E-05 0.00 4.28E-05 0.00 WA 0.00 0.00 4.28E-05 0.00 6.83E-04 0.00 0.00E+00 0.00 0.00
S rene 100-42-5 TAP/HAP 2.00E-05 0.00 2.00E-05 0.00 WA 0.00 0.00 2.00E-05 0.00 WA 0.00 0.00E+00 0.00 0.00
Tetrachloroethene 127-18-4 TAP/HAP 2.80E-06 0.00 2.80E-06 0.00 WA 0.00 0.00 2.80E-06 0.00 WA 0.00 0.00E+00 0.00 0.00
Toluene 108-88-3 TAP/HAP 1.60E-04 0.00 1.60E-04 0.00 WA 0.00 0.00 1.60E-04 0.00 6.20E-03 0.00 0.00E+00 0.00 NO
Total Fluorides 1 16984-488 TAP I 4.48E-01 0.00 4.48E-01 0.00 WA 0.00 0.00 4.48E-01 0.00 WA 0.00 O.OgE+00 0.00 1 0.00
%ylene 1330-20-7 TAP/HAP I 1.25E-04 0.00 1.25E-04 0.00 WA 0.00 0.00 125E-04 0.00 1.09E-04 0.00 0.00E+00 0.00 1 0.00
1. Emission factor based on USEPA/Bdck Auociation of North Carolina sponsored source test completed at Triangle Brick Company's Merry Oaks,North Carolina facility.
1a.Emission factor for TSP based on Stack Test dated August 2006.PM-10 set equal to TSP due to AERO limitation..
2. Emission factors obtained from AP42 Section 11.3"Brick and Structural Clay Products",Final report,August 1997.
3. Uncontrolled emission factor for Hydrogen Fluoride and Hydrogen Chloride based on source test completed August 2006.DIA was operated a few days each month to maintain it,but the associated reduction is not accounted for in these calculations.
4. Fuel combustion emission factors obtained from AP42 Section 1.3"Fuel Oil Combustion"and NCDEM guidance.
5. Heat input rating assumed to be 140,000 Btu/gallon for W.2 fuel oil and 150,000 Btu/gal for No.6 fuel oll.
6. Sulfur content of No.2 fuel oil assumed to be 0.5%.
7. Sulfur content of No.6 Kiel oil assumed to be 2.1 0.
8. Emission factor for Total Fluorides is(1.6)z(Hydrogen Fluoride emission factor).
2 of

Table A-3
Calculation of Actual 2014 Air Emissions From Brick Tunnel Kiln#3
(Source I.D.-K-3)
Triangle Brick Company
Merry Oaks,North Carolina
Production Data
Tons of Fired Brick Produced I 133 368 tons
Cubic Feet Natural Gas Combusted 229 341,000
Gallons Distillate Oil Combusted 3,483 gallons
Gallons Residual Oil Combusted 0gallons
Tons Brick Fired With Natural Gas 133093 tons
Tons Brick Fired WM Distillate Oil 275 tons
Tons Brick Fired Wth Residual Oil 1 0 tons
Primary Operating Scenario Second Operating Scenaro Tertiary Operating Operabng Scenario Emissions Summary
NC TAP Wor Clav Firina i Net.Gas Clay Firing Not.Gas Distillate Fuel Combustion Total ClaV Firing Nat,Gas Residual Fuel Combustion Total
Pollutant CAS Number HAP Emission Actual Emission Actual Emission Actual O er.Scan. Emission Actual Emission Actual O er.Scen. Total 2014 Total 2014
Factor Emission Rate Factor Emission Rate Factor Emission Rate Emissions Factor Emission Rate Factor Emission Rate Emissions Emissions Emissions
Iba/ton Ibs r Ibs/ton) (lbs r) (lb/1000gallon) (Ibs/yr) (ibs r Ibsrt- Iba r Ib/1000 all.. Qbs/yr Iba r) (Ibs) (tons)
TSP Neither 0.3769 50,156.28 0.3796 104.29 2.0 6.97 111.26 D.3796 0.00 22.5 0.00 0.00 50.267.53 25.13
PM-10' Neither 0.3769 50,156.28 0.3796 104.29 1.1 3.76 108.05 0.3796 0.00 19.6 0.00 0.00 50.264.33 25.13
PM-2.5 Neither 0.3769 50,156.28 0.3796 104.29 1.1 3.76 108.05 0.3796 0.00 19.6 0.00 0.00 50,264.33 25.13
S02 Neither 0.0627 8,344.95 0.0627 17.23 71.0 247.29 264.52 0.0627 0.00 329.7 0.00 0.00 8,609.47 4.30
NO.' Neither 0.126 16,769.75 0.126 34.62 20.0 69.66 104.28 0.126 0.00 55.0 0.00 0.00 16,874.03 8.44
CO Neither 0.577 76,794.81 0.577 158.52 5.0 17.42 175.94 0.577 0.00 5.0 0.00 0.00 76,970.75 38.49
VOG Neither 0.0568 7,559.70 0.0568 15.61 0.2 0.70 16.3D 0.0568 0.00 0.3 0.00 0.00 7,576.00 3.79
1,1,1 Trichloroethane 71-55-6 TAP/HAP 4.70E-06 0.63 4.70E-06 0.00 WA 0.00 0.00129 4.70E-06 0.00 N/A 0.00 0.00 0.63 0.00
1.4 Dichlorobenzene 10646-7 TAP/HAP 4.80E-05 6.39 4.80E-05 0.01 N/A 0.00 0.01319 4.80E-05 0.00 N/A 0.00 0.00 6.40 0.00
2-Butanone MEK 78-93-3 TAP/HAP 2.20E-04 29.28 2.20E-04 0.06 WA 0.00 0.06044 2.20E-04 0.00 WA 0.00 0.00 29.34 0.01
2-Hexanone MIBKT 591-78-6 TAP/HAP 8.50E-05 11.31 8.50E-05 0.02 WA 0.00 0.02335 8.50E-05 0.00 N/A 0.00 0.00 11.34 0.01
Acetone 67-64-1 Neither 1.70E-03 226.26 1.70E-03 0.47 WA 0.00 0.46705 1.70E-03 0.00 N/A 0.00 0.00 226.73 0.11
AnOmon SBC-Omer HAP 6.38E-05 8.49 6.38E-05 0.02 N/A 0.00 0.01753 6.38E-05 0.00 5.25E-03 0.00 0.00 8.51 0.00
Arsenic ASC-Other TAP/HAP 2.29E-05 3.05 2.29E-05 0.01 5.92E-04 0.00 0.00835 2.29E-05 0.00 1.32E-03 0.00 0.00 3.06 0.00
Benzene 7143-2 TAP/HAP 2.90E-03 385.97 2.90E-03 0.80 N/A 0.00 0.79674 2.90E-03 0.00 2.14E-04 0.00 0.00 366.77 0.19
Benz.a rene POM POM TAP N/A 0.00 WA 0.00 3.30E-03 0.01 0.01149 N/A 0.00 1.20E-03 0.00 0.00 0.01 0.00
Be lium 7440-41-7 TAP/HAP 4.27E-07 0.06 4.27E-07 0.00 3.53E-04 0.00 0.00135 4.27E-07 0.00 2.78E-05 0.00 0.00 0.06 0.00
Bis -ethylheqQ Phthalate 117-81-7 HAP 2.00E-03 266.19 2.00E-03 0.55 N/A 0.00 0.54948 2.00E-03 0.00 WA 0.00 0.00 266.74 0.13
Bu en hthalate 85-68-7 Neither 1.80E-05 2.40 1.80E-05 0.00 WA 0.00 0600495 1.80E-05 0.00 WA 0.00 0.00 2.40 0.00
Cadmium 7440-43-9 TAP/HAP 5.76E-06 0.77 5.76E-06 0.00 1.55E-03 0.01 0.00698 5.76E-06 0.00 3.98E-04 0.00 0.00 0.77 0.00
Carbon Disulfide 75-15-0 TAP/HAP 4.10E-05 5.72 4.30E-05 0.01 WA 0.00 0.01181 4.30E-05 0.00 WA 0.00 0.00 5.73 0.00
Chlorine 7782505 TAP/HAP 1.30E-03 173.02 1.30E-03 0.36 N/A 0.00 0.35716 1.30E-03 0.00 N/A 0.00 0,00 173.38 0.09
Chloroethane 75-00-3 HAP 5.70E-04 75.86 5.70E-04 0.16 N/A 0.00 0.15660 5.70E-04 0.00 N/A 0.00 0.00 76.02 0.04
Chloromethane 7457-3 HAP 6.70E-04 89.17 6.70E-04 0.18 N/A 0.00 0.18407 6.70E-04 0.00 N/A 0.00 0.00 89.36 0.04
Chrome VI NSCR6-Othef TAP/HAP WA 0.00 N/A 0.00 2.38E-03 0.01 O.0 a29 N/A 0.00 2.48E-04 0.00 0.00 0.01 0.00
Chromium CP.C-Oth,eI HAP 2.09E-OS 2.78 2.09E-05 0.01 8.11E-03 0.03 0.03399 2.09E-05 0.00 8.45E-04 0.00 0.00 2A2 0.00
1 of 2

Table A-3
Calculation of Actual 2014 Air Emissions From Brick Tunnel Kiln#3
(Source I.D.-K-3)
Triangle Brick Company
Merry Oaks,North Carolina
Production Data
Tons of Fired Brick Produced 131368 tons
Cubic Feet Natural Gas Combusted 229 341,000 ip
Gallons Distillate Oil Combusted 3,483 gallons
Gallons Residual Oil Combusted 0 gallons
Tons Brick Fired Nth Natural Gas 133093 tans
Tons Brick Fired Aft Distillate Oil 275 tons
Tons Brick Fired Nth Residual Oil 0 tans
Primary Operating Scenario Secondery Operating Operafing Scenario Tertiary Operating Scenario Emissions Summary
NC TAP Wor Cla Firin Nat.Gas) ClayFiringNet.Gas Disfi(late Fuel Combustion- Total ClayFiringNat.Gas J4,25E-02
uel Combustion Total
Pollutant CAS Number HAP Emission Actual Emission Actual Emission Actual O er.Scan. Emission Actual n Actual O er.Scan. Total 2014 Total 2014
Factor Emission Rate Factor Emission Rate Factor Emission Rate Emissions Factor Emission RateEmission Rate Emissions Emissions Emissions
Ibs/ton (Ihs r) (libation) (Ib r) (lb/1000 allon (lbs/yr (lbs r Ibshon) Ibetyr) eon Ibs r) Ibs r (Ibri (tons)
Cobalt COC-other HAP 4.27E-06 0.57 4.27E-06 0.00 NIA 0.00 0.D0117 4.27E-06 0.00 3 0.00 0.00 0.57 0.00
Di Butyl Phthalate 84-74-2 HAP 1.40E-04 18,63 1.40E-04 0.04 N/A 0.00 0.03846 1.40E-04 0.000.00 0.00 18.67 0.D1
Diets hthalate 84-66-2 Neither 2.40E-04 31.94 2.40E-04 0.07 WA 0.00 0,06594 2.40E-04 O.DOO.DO 0.00 32.01 0.02
EthylBenzene 100-41-4 HAP 4.40E-05 5.86 4.40E-05 0.01 N/A 0.00 0.01209 4.40E-05 0.00 S 0.00 0.00 5.87 0.00
Formaldeh de 50-00-0 TAP/HAP WA 0.00 N/A 0.00 4.80E-02 0.17 0.16718 N/A 0.00 2 0.00 0.00 0.17 0.00
H dro en Chloride 7647-Ot-0 TAP/HAP 0.1700 22,625.85 1.70E-01 46.71 N/A 0.00 46.70545 1.70E-01 0.00 NIA 0.00 O.DO 22.672.56 11.34
Hydrogen Fluoride 7664-39-3 TAP/HAP 0.2800 37.266.11 2.80E-01 76.93 N/A 0.00 76.92663 2.80E-01 0.00 NIA 0.00 0.00 37,343.04 18,67
Iodomethare 74-88-4 HAP 9.30E-05 12.38 9.30E-05 0.03 N/A 0.00 0.02555 9.30E-05 0.00 NIA 0.00 0.00 12.40 0.01
Lead' PBC-Other' HAP 1.50E-04 19.96 1.50E-04 0.04 1.25E-03 0.00 0.04556 1.50E-04 0.00 1.51E-03 0.00 0.D0 20.01 0.01
Men anese MNC-Other TAP/HAP 8.46E-05 1126 8.46E-05 0.02 1.97E-03 0.01 0403010 8.46E-05 0.00 3.00E-03 0.00 0.00 1129 0.01
Mercu 7439-97-6 TAP/HAP 1.00E-05 1.33 1.00E-05 0.00 4.23E-04 0.00 0400422 1.00E-05 0.00 1.13E-04 0.00 0Ao 1.34 0.00
Naphthalene' 91-20-3 HAP 6.50E-05 8.65 6.50E-05 0.02 N/A 0.00 0.01786 6.50E-05 0.00 1.13E-03 0.00 0.00 8.67 0.00
Nickel 7440-02-0 TAP/HAP 1.28E-05 1.70 1.28E-05 0.00 2.40E-02 0.08 0408711 1.28E-05 0.00 8.45E-02 0.00 0.00 1.79 0.00
Phenol 108.95-2 TAP/HAP 8.60E-05 11.45 8.60E-05 0.02 N/A 0.00 0402363 8.60E-05 0.00 NIA 0.00 0.00 11.47 0.01
Selenium SEC HAP 4.28E-05 5.70 4.28E-D5 0.01 WA 0.00 0.01176 4.28E-05 0.00 6.83E-04 0.00 0.00 5.71 0.00
Styrene' 100-42-5 TAP/HAP 2.00E-05 2.66 2.00E-05 0.01 N/A 0.00 0.00549 2.00E-05 0.00 N/A 0.00 0.00 2.67 0.00
Tetrachloroethene 127-18-4 TAP/HAP 2.80E-06 0.37 2.80E-D6 0.00 N/A 0.00 0.00077 2.80E-06 0.00 N/A 0.00 0.00 0.37 0.00
Toluene 108-88-3 TAP/HAP 1.60E-04 21.2925 78 1.60E-04 0.04 N/A 0.00 0.04396 1.60E-04 0.00 6.20E-03 0.00 0.00 21.34 0.01
Total Fluorides 16984-48-8 TAP 4.48E-01 59 6, . 4.48E-01 123.08 WA 0.00 123.08260 4.48E-01 0.00 N/A 0.00 0.00E+00 59,748.86 29.87
Xylene 1330-20 7 TAP/HAP 1.25E-04 16.64 1.25E-04 0.03 NIA 0.00 0.03434 1.25E-04 0.00 1.09E-04 0.00 0.00 1fi.67 0.01
1. Emission factor based on USEPA/Brick Association of North Carolina sponsored source test completed at Triangle Brick Company's Merry Oaks,North Carolina facility.
1 a.Emission factor for TSP based on Stack Test dated April and May 2006.PM-10 set equal to TSP due to AERO limitation.
2. Emission factors obtained from AP-42 Section 11.3"Brick and Structural Clay Products",Final report,August 1997.
3. Uncontrolled emission factor for Hydrogen Fluoride and Hydrogen Chloride based on source test completed August 2006.DLA was operated a few days each month to maintain it,but the associated reduction is not accounted for in these calculations.
4. Fuel combustion emission factors obtained from AP-42 Section 1.3"Fuel Oil Combustion"and NCDEM guidance.
5. Heal input rating assumed to be 140,000 Btu/gallon for No.2 fuel oil and 150,000 Btu/gal for No.6 fuel oil.
6. Sulfur content of No.2 fuel oil assumed to be 0.5%.
7. Sulfur content of No.6 fuel oil assumed to be 2.1%.
8. Emission factor for Total Fluorides is(1.6)x(Hydrogen Fluoride emission factor).
2 of

Table A-4
2014 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
2014 Natural Gas Combusted- Kiln#1: 2,287,000 ft3
2014 Natural Gas Combusted-Kiln#2: 0 ft3
2014 Natural Gas Combusted-Kiln#3: 229,341,000 ft3
Formaldehyde Emission Factor: 0.075 Ib/10e06 ft3
Emission Calculations -Kiln#1
Formaldehyde(lb/yr) = 2287000 ft3 x 0.075 Ib/10e06 ft3
0.17153 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) = 229341000 ft3 x 0.075 lb/10e06 ft3
_ . 17.201 lb formaldehyde/yr
Total Formaldehyde Emissions-Kiln#1, Kiln#2, and Kiln#3
Formaldehyde (lb/yr) = 17.37 lbs Formaldehyde/yr
1.NCDAQ Natural Gas Combustion Emissions spreadsheet

h
4r
Table A-5
2014 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/yr) 8,760
Natural Gas Combusted(ft)
Sand Processed (tpy)
Emission E
,. .,mission. Emisstorr
Pollutant Factor Rate Rate
E .` .... ... .. ...: d ..
Ib/MMsc (Ib/hr) (tPY)
NOX 1 3.65E-06 1.60E-05
CO 0.84 3.07E-06 1.34E-05
SO2 0.006 2.19E-08 9.59E-08
VOC 0.055 2.01 E-07 8.79E-07
Formaldehyde 0.00075 2.74E-09 1.20E-08
Emission2 -.Emission::- - Emission
Po[[utant ,Factor? = Rate Rate
(lb/ton .(Ib/hr) (tpy)
PM 0.02 2.70E-03 1.18E-02
PM10 1 0.02 1 2.70E-03 1 1.18E-02
PM2.5 0.02 2.70E-03 1 1.18E-02
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 2014 Air Emissions from Crushing,Screening,and Grinding Operations
(Source I.D. PC1-PC6 CG1 -CG49)
Triangle Brick Company
Merry Oaks, North Carolina
Actual = Actual
'-
Emission Annual
Soufdb.,---.
n miss
Unit —n id' E lon: Em issibW
Factor
tons Ratiji blyr)-:�i-k ton
1 1 - - /yr),
PM-2.5 3 5.90E-02 lbs/ton 175,484 10,354 5.18
Primary Crushing4 PM-1 0 5.90E-02 lbs/ton 175,484 10,354 5.18
pM3 5.90E-02 lbs/ton 175,484 -10,354 5.18
PM-2.5:' 0.0023 lbs/ton 175,484 404 0.20
Grinding&Screening PM-1 0 0.0023 lbs/ton 175,484 -404 0.20
PM 0.025 , lbs/ton , 175,484 4,387 2.19
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 brick.
3. PM2.5(and PM for primary crushing)emission factors not determined in AP-42.Assumed emission factors=P10 emission
factor.
4.PM-1 0 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
2014 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 2,287,000 ft3
MOK2 /A ft3
MOK3 1`+ifA ft3
Emission Emission Rate
Pollutant ; Factor .' (Ibs/yr) TotaI.MO'
(Ib/106 ft3) MOK1 MOK2 MOK3.
NOx 100 228.7 N/A N/A 228.7
CO 84 192.108 N/A N/A 192.108
PM (Total)2 7.6 17.3812 N/A N/A 17.3812
S02 0.6 1.3722 WA NIA 1.3722
TOC 11 25.157 N/A N/A 25.157
VOC 5.5 12.5785 NIA NIA 12.5785
Acetaldehyde(H,T)** 0.0000152 3.48E-05 N/A NIA 3.48E-05
Acrolein (H,T)** 0.000018 4.12E-05 NIA WA 4.12E-05
Ammonia T** 3.2 7.3184 NIA NIA 7.3184
Arsenic H, 0.0002 0.000457 NIA WA 0.000457
Benzene(H,T) 0.0021 0.004803 NIA N/A 0.004803
Benzo a p rene(H,T) 0.0000012 2.74E-06 N/A N/A 2.74E-06
Beryllium (H,T) 0.000012 2.74E-05 NIA N/A 2.74E-05
Cadmium H,T) 0.0011 0.002516 NZA N/A 0.002516
Chromium (VI) (H,T) 0.0014 0.003202 N/A NIA 0.003202
Cobalt(H) 0.000084 0.000192 NZA N/A 0.000192
n-Hexane (H,T) 1.8 4.1166 N/A MIA 4.1166
Lead (H) 0.0005 0.001144 N/A WA 0.001144
Manganese(H,T) 0.00038 0.000869 NIA NIA 0.000869
Mercury H,T 0.00026 0.000595 NIA N/A 0.000595
Na thalene H 0.00061 0.001395 NIA NIA 0.001395
Nickel H,T 0.0021 0.004803 NZA N/A 0.004803
Selenium H 0.000024 5.49E-05 NIA NIA 5.49E-05
Toluene (H,T) 1 0.0034 10.0077761 N:'T I N/A 0.007776
1.NCDAQ Natural Gas Combustion Emissions spreadsheet
2.PM(Total)is assumed to be PM2.5=PM10

Table A-8
2014 Air Emissions Inventory
Supporting Emissions Calculations
VOC Emissions from Tanks
Triangle Brick Company-Merry Oaks Facility
Annual Throughputs(gallons)
Additive A Tank 79,425
Gasolme Tank 2 9,487
No 2'Fue101 31483
No t%':FuelAl 0
Tanks 4.09d Run Results
Additive A Tank
—(Ibs) -
;Components Working :. Breathing Total
Loss Loss °' Emissions
Calcium L'ig'�osulfonate. 252.82 531.99 784.81
Gasoline Tank
-1/OC.(Ibs
Components; Working Breathing Total
'Loss .. Loss `.Emissions =-
Gasoline(RVP 7) 60.98 287.13 348.11
No. 2 Fuel Oil Tank 1
VOC(Ibs)
Components; ` i Working Breathing, Total
Loss Loss'` iEmissions .
No..2'_Fue[Di1 0.02 3.98 4
No.2 Fuel Oil Tank 2
OC{Ibs)-
Components Working Breathing Total
Loss Loss Emissions:_
No:-2 Fuel,Oil,_ 0.02 3.98 4
No.2 Fuel Oil Tank 3
VOC!(lbs)
'Components` .Working Breathing, Total
Loss ;Loss Emissions
No.2 Fuel Oil 0.02 3.98 4
No.6 Fuel Oil Tank
Components ..,Work! =' Breathing Total
Loss LOSS,;101, missionsmil
No:6; el.O t 0 0.04 0.04

Table A-9
2014 Emissions Summary
Triangle Brick Company
Merry Oaks Facility
Triangle Brick Company
Durham, North Carolina
NC TAP 2014 Z014
Pollutant Emissions Emissions,:
woe HAP .
Ib/ r to61 r
TSP Neither 65,049 32.52
PM-10 Neither 61,063 30.53
SO2 Neither 8,611 4.31
NOx Neither 17,103 8.55
CO Neither 77,163 38.58
TOC Neither 25 0.01
VOC Neither 8,734 4.37
1,1,1 Trichloroethane TAP/HAP 0.63 3.13E-04
1 A Dichlorobenzene TAP/HAP 6.40 3.20E-03
2-Butanone MEK) TAP/HAP 29.34 1.47E-02
2-Hexanone(MIBK) TAP/HAP 11.34 5.67E-03
Acetaldehyde TAP/HAP 0.00 1.74E-08
Acetone Neither 226.73 1.13E-01
Aorolein TAP/HAP 0.00 2.06E-08
Ammonia TAP 7.32 3.66r=--03
Antimony HAP 8.51 4.25E-03
Arsenic TAP/HAP 3.06 1.53E-03
Benzene TAP/HAP 386.77 1.93E-01
Benzo(a)p rene(POM) TAP 0.01 5.75E-06
Beryllium TAP/HAP 0.06 2.91 E-05
Bis(2-eth the I) Phthalate HAP 266.74 1.33E-01
Butylbenzylphthalate Neither 2.40 1.20E-03
Cadmium TAP/HAP 0.78 3.88E-04
Carbon Disulfide TAP/HAP 5.73 2.87E-03
Chlorine TAP/HAP 173.38 8.67E-02
Chloroethane HAP 76.02 3.80E-02
Chloromethane HAP 89.36 4.47E-02
Chrome VI TAP/HAP 0.01 4.14E-06
Chromium HAP 2.82 1.41 E-03
Cobalt HAP 0.57 2.85E-04
Di Butyl Phthalate HAP 18.67 9.34E-03
Dieth (phthalate Neither 32.01 1.60E-02
Ethyl Benzene HAP 5.87 2.93E-03
Formaldehyde TAP/HAP 17.54 8.77E-03
n-Hexane TAP/HAP 4.12 2.06E-03
Hydrogen Chloride TAP/HAP 22,672.56 1.13E+01
Hydrogen Fluoride TAP/HAP 37,343.04 1.87E+01
lodomethane HAP 12.40 6.20E-03
Lead HAP 20.01 1.00E-02
Manganese TAP/HAP 11.29 5.65E-03
Mercury TAP/HAP 1.34 6.68E-04
Naphthalene HAP 8.67 4.34E-03'
Nickel TAP/HAP 1.80 8.98E-04
Phenol TAP/HAP 11.47 5.73E-03
Selenium HAP 5.71 2.85E-03
Styrene TAP/HAP 2.67 1.33E-03
Tetrachloroethene TAP/HAP 0.37 1.87E-04
Toluene TAP/HAP 21.35 1.07E-02
Total Fluorides TAP 59,748.86 1.13E+01
X lene TAP/HAP 16.67 8.34E-03

TANK 4.09D RUNS
TRIANGLE BRICK COMPANY-MERRY OAKS

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 T hroughput(gal/yr): 0.00
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 psis)
file:///C:/Program%2OFiles/Tanks4O9d/summarydisplay.htm 6/19/2015

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) MCI. Mass Mass Mol. Basis for Vapor Pressure
Mixture/Component 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 190.000D 387.00 Option 1:VP60=.00004 VP70=.00006
file:///C:/Program0/`2OFiles/Tanks4O9d/summarydisplay.htm 6/19/2015

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(lb): 0.0363
Vapor Space Volume(cu ft): 1.789.5488
Vapor Density(lb/cu ft): 0.0000
Vapor Space Expansion Factor. 0.0386
Vented Vapor Saturation Factor: 1.0000
Tank Vapor Space Volume:
Vapor Space Volume(cu ft): 1,789.5488
Tank Diameter(ft): 12.0000
Vapor Space Outage(ft): 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): 12.0000
Shell Radius(ft): 6.0000
Vapor Density
Vapor Density(lb/cu it): 0.0000
Vapor Molecular Weight(Ib/lb-mole): 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
(psia cult/(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(Btu/sgft day): 1,393.0797
Vapor Space Expansion Factor
Vapor Space Expansion Factor: 0.0386
Daily Vapor Temperature Range(deg.R): 22.2671
Daily Vapor Pressure Range(psia): 0.0000
Breather Vent Press.Setting Range(psia): 0.0600
Vapor Pressure at Daily Average Liquid
Surface Temperaturd(psia): 0.0000
Vapor Pressure at Daily Minimum Liquid
Surface Temperature(psia): 0.0000
Vapor Pressure at Daily Maximum Liquid
Surface Temperature(psia): 0.0001
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: 1.0000
Vapor Pressure at Daily Average Liquid:
Surface Temperature(psia): 0.0000
Vapor Space Outage(ft): 15.8231
Working Losses(lb): 0.0000
file:///C:/Program%2OFiles/Tanks4O9d/summarydisplay.htm 6/19/2015

TANKS 4.0 Report Page 4 of 7
Vapor Molecular Weight(lb/lb-mole): 190.0000
Vapor Pressure at Daily Average Liquid
Surface Temperature(psia): 0.0000
Annual Net Throughput(gal/yr.): 0.0000
Annual Turnovers: 0.0000
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): 0.0363
file:///C:/Program%2OFiles/Tanks4O9d/summarydisplay.htm 6/19/2015

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(lbs)
Components Working Lossil Breathing Loss Total Emissions
Residual oil no.6 0.001 0.04�� 0.04
file:///C:/Program%20FIles/Tanks4O9d/summarydisplay.htm 6/19/2015

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
City: Raleigh
State: North Carolina
Company:
Type of Tank: Vertical Fixed Roof Tank
Description: 3 tanks
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: 0.05
Net Throughput(gaVyr): 1,161.00
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)
file:///C:/Program%2OFiles/Tanks4O9d/summarydisplay.htm 6/19/2015

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-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 Mal. Basis for Vapor Pressure
Mixture/Component 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 0.0068 0.0056 0.0082 130.0000 188.00 Option 1:VP60=.0065 VP70=.009
file:///C:/Program%2OFiles/Tanks4O9d/summarydisplay.htm 6/19/2015

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-Vertical Fixed Roof Tank
Raleigh;North Carolina
Annual Emission Calcaulations
Standing Losses(lb): 3.9805
Vapor Space Volume(cu ft): 1,789.5488
Vapor Density(lb/cu ft): 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(ft): 12.0000
Vapor Space Outage(ft): 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): 12.0000
Shell Radius(ft): 6.0000
Vapor Density
Vapor Density(lb/cu ft): 0.0002
Vapor Molecular Weight(lb/lb-mole): 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
(psia cuft/(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: 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(psta): 0.0082
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): 0.0244
file:///C:/Program%2OFiles/Tanks4O9d/summarydisplay.htm 6/19/2015

TANKS 4.0 Report Page 4 of 7
Vapor Molecular Weight(IbAb-mole): 130.0000
Vapor Pressure at Daily Average Liquid
Surface Temperature(psia): 0.0068
Annual Net Throughput(gal/yr.): 1,161.0000
Annual Turnovers: 0.0464
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): 4.0049
file:///C:/Program%2OFiles/Tanks4O9d/summarydisplay.htm 6/19/2015

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 -Vertical Fixed Roof Tank
Raleigh, North Carolina
Losses(lbs)
Components Working Lossil Breathing Loss Total Emissions
Distillate fuel oil no.2 0.0211 3.981 L--> Q,©O-z-
V'Or
file:///C:/Program%2OFiles/Tanks4O9d/summarydisplay.htm 6/19/2015

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 Gasoline Tank
City: Raleigh
State: North Carolina
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: 3.16
Net Throughput(gal/yr): 9,487.00
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)
file:///C:/Program%2OFiles/Tanks4O9d/summarydisplay.htm 5/15/2015

TANKS 4.0 Report Page 2 of 6
TANKS 4.0.9d
Emissions 'Report - Detail Format
Liquid Contents of Storage Tank
Merry Oaks Gasoline 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 MCI. Basis for Vapor Pressure
Mixture/Component Month Avg. Min. Max. (deg F) Avg. Min. Max. Weight. Fract. Fract. Weight Calculations
Gasoline(RVP 7) All 66.48 57.31 75.66 61.52 3.9699 3.2977 4.7489 68.0000 92.00 Option 4:RVP=7,ASTM Slope=3
file:///C:/Program%20Files/Tanks.4O9d/summarydisplay.htm 5/15/2015

TANKS 4.0 Report Page 3 of 6
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(cu ft): 294.8516
Vapor Density(Ib/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(ft): 5.5000
Vapor Space Outage(ft): 12.4105
Tank Shell Height(ft): 18.0000
Average Liquid Height(ft): 9.0000
Roof Outage(ft): 3.4105
Roof Outage(Dome Roof)
Roof Outage(ft): 3.4105
Dome Radius(ft): 5.5000
Shell Radius(ft): 2.7500
Vapor Density
Vapor Density(lb/cu ft): 0.0478
Vapor Molecular Weight(lb/lb-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 R
(psia cuft/(lb-mol-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(Btu/Sgft day): 1.393.0797
Vapor Space Expansion Factor
Vapor Space Expansion Factor. 0.2015
Daily Vapor Temperature Range(deg.R): 36.6994
Daily Vapor Pressure Range(psia): 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
Daily 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): 12.4105
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TANKS 4.0 Report Page 4 of 6
Working Losses(lb): 60.9776 .
Vapor Molecular Weight(lb/lb-mole): 68.0000
Vapor Pressure at Daily Average Liquid
Surface Temperature(psia): 3.9699
Annual Net Throughput(gal/yr.): 9,487.0000
Annual Turnovers: 3.1623
Turnover Factor: 1.0000
Maximum Liquid Volume(gal): 3,000.0000
Maximum Liquid Height(ft): 18.0000
Tank Diameter(ft): 5.5000
Working Loss Product Factor. 1.0000
Total Losses(lb): 348.1121
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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 Gasoline Tank-Vertical Fixed Roof Tank
Raleigh, North Carolina
Losses(lbs)
Components Working Lossil Breathing Loss Total Emissions
Gasoline(RVP 7) 60.98 287.13 348.11
/o ccz;ri n Zell w, Q &i 6&1- '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 Additive A 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: 3.18
Net Throughput(gal/yr): 79,425.00
Is Tank Heated(y/n): N
Paint Characteristics
Shell Color/Shade: White/White
Shell Condition Good
Roof Color/Shade: WhiteAAlhite
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 6
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) Mol. Mass Mass MCI. Basis for Vapor Pressure
Mixture/Component Month Avg. Min. Max. (deg F) Avg. Min. Max. Weight. Fract. 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 6
.c r•
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(lb): 531.9875
Vapor Space Volume(cu ft): 1,789.5488
Vapor Density(lb/cu ft): 0.0239
Vapor Space Expansion Factor. 0.0413
Vented Vapor Saturation Factor: 0.8250
Tank Vapor Space Volume:
Vapor Space Volume(cu ft): 1,789.5488
Tank Diameter(ft): 12.0000
Vapor Space Outage(ft): 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): 12.0000
Shell Radius(ft): 6.0000
Vapor Density
Vapor Density(lb/cu ft): 0.0239
Vapor Molecular Weight(IbIlb-mole): 528.6100
Vapor Pressure at Daily Average Liquid
Surface Temperature(psia): 0.2529
Daily Avg.Liquid Surface Temp.(deg.R): 520.8354
Daily Average Ambient Temp.(deg.F): 59.2833
Ideal Gas Constant R
(psia cuft/(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(Btu/sgft day): 1,393.0797
Vapor Space Expansion Factor
Vapor Space Expansion Factor. 0.0413
Daily Vapor Temperature Range(deg.R): 22.2671
Daily Vapor Pressure Range(psia): 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(psia): 0.2668
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(ft): 15.8231
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TANKS 4.0 Report Page 4 of 6
c ,rr
Working Losses(lb): 252.8224
Vapor Molecular Weight(lb/Ib-mole): 528.6100
Vapor Pressure at Daily Average Liquid
Surface Temperature(psia): 0.2529
Annual Net Throughput(gal/yr.): 79,425.0000
Annual Turnovers: 3.1770
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): 784.8099
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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 Additive A Tank-Vertical Fixed Roof Tank
Raleigh, North Carolina
Losses(lbs)
Components Working Loss Breathing Loss Total Emissions
Calcium Lignosulfonate 252.82 531.99 784.81
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