AQ_F_1900009_20190627_EI_Cmb-EI-File

REGIONAL QAPP Audit Form: Point Source EI CY 2018
Facility Name: General Shale Brick, Inc.- Moncure Facility Facility ID: 1900009
Permit Number: 04384T39 Assigned to: Stanley Williams Confidential Coopy�S bmitted?
Region: RRO O YES P NO
Initial Review/Data Entry
tter date received into ED.
Pceipt of EI properly documented
R' I submitted through AERO,Receipt of Certification form entered in ED
s EI received by June 30 deadline. If not,was the failure to meet the deadline documented?
Id D entry complete date at entered_06/14/2019
e Approval Due:_10/31/2019 Date Approved:_09/10/2019
Comments: Brick production for 2018 was up 2.496 percent from the brick production in 2017. Emission factors for
hydrogen fluoride,hydrogen chloride, and total fluorides have been corrected to reflect the SSCB approved test results for the
Kiln 4 test that took place on September 24,2015 that established the site specific emission factors for these pollutants. Kiln 4
was the only kiln that operated in CY 2018.
Inventoa Audit (verify that the checks below at a minimum have been investigated and documented).
ijs�fffissions
ve forms appear to be complete.
ification form was signed by appropriate official.
reported for all sources(permitted,insignificant,and unpermitted)or marked as not operated or NRTR.
Wr Supporting calculations, control and/or capture efficiencies and emission factor documentation included and appears
ect.
0 known OSs,control devices and release points reported for each emission source.
4 1 emissions above de minimus levels have been reported for all emission sources.
Lff'
,ssion Factors are best available/most current.
W lculations and facility totals add up correctly.
QA/QC issues addressed.
L-9'9 bvious outlier data(>10%difference)have been investigated and explained in writing.
W'�All changes/corrections were made to the inventory and documented either on paper or DataEntryMain page.
U-tomments entered on DataEntryMain page(if any)are adequate for communication(comments make sense).
Auditor signature Date: tv
'4
Comments: - 7
Corrective action recommended to Reviewer:
Reviewer signature�7 '0 Date:-9• i 2 •Za19

2018 Emissions Inventory Review / Data Tracking Form
Facility Name: General Shale Brick Inc. - Moncure Facility Facility ID: 1900009
Facility Assigned to: Data Entry: Chatham County
Classification: Stanley Williams Confidential Copy Submitted?
Title V 0 YES
NO
Initial Review/Data Entry
e Enter date received into ED. Date Received:
Ci Assigned to appropriate individual. Date Assigned: Date Due:
0 Paper copy submitted: One copy received with supporting documentation,certification form signed by responsible official,and
appears generally complete;OR
Electronic copy submitted: All supporting documentation and certification form(with time/date stamp)signed by responsible
official has been received.
Comments:
Inventory Review
0 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.
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.
e Check if SCC codes for each OS are accurate and update if needed.
0 Evaluate"U"sources for significance and address according to policy.
to 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.
2 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,AP42,etc.).
0 Review facility comments and address any issues.
0 Update ED(Data Entry Main)if additionabinformation 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.
0 Put inventory review comments and summarize any changes in ED-Data Entry Main"DAQ internal comments".
0 Print and attach the facility total report.
Date Info Requested: Date Info Received: Total Days on Hold:
Date Review Complete: $•2 • 2p/Q Signature:
Date Submitted to EI Coordinator: $• �$. Q,p/Q
Date Approved: W Initials:

Facility Total CY 2018 Emission Summary Recorded in ED Facility ID #: 1900009
Facility Name: General Shale Brick, Inc. -Moncure Facility Permit#(s): 04384139
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 2018 CY 2017 Demini- %
from ED from Fees mus Change
CO Co 84.70 82.42 0.5 2.8%
NOx Nox 3.3.30- 32.39 0.5 2.8%
PM(TSP) TSP 69.62 66.78 0.5 4.3%
PM10 PM10 66.33 64.42 0.5 3.0%
PM2.5 PM2.5 66.27 64.38 0.5 2.9%
SO2 S02 0.850000 0.830000 0.5 2.4%
VOC VOC 4.68 4.57 0.5 2.4%
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPS) (Pounds/Year)
Pollutant CAS CY 2018 CY 2017 Demini- %
from ED from Fees mus Change
Arsenic& Compounds(total mass of elemental AS, arsine and 4.61 4.49 0.01 12.7
all inorganic compounds)
Arsenic Unlisted Compounds- Specify Compound ASC-other 4.61 4.49 0.01 2.5%
(Component of ASC)
Cadmium & compounds(total mass includes elemental metal) 2.23 2.17 0.1 12.8%
Cadmium Metal, elemental, unreacted(Component( 7440-43-9 2.23 2.17 0.1 2.5%
CDC)
Chromium-All/Total(includes Chromium (VI) categories, Z58 Z39 0.1 2..6%
metal and others)
Chromic acid (VI) (Component of SolCR6 & CRC) 7738-94-5 7.58 7.39 0.01 2.5%
Chromium (VI)Soluble Chromate Compounds (Component of 7.58 7.39 0.01 2,6%
CRC)
08/28/2019 Page 1 of 3

Facility Total CY 2018 Emission Summary Recorded in ED Facility ID#: 1900009
Facility Name: General Shale Brick. Inc. -Moncure Facility Permit#(s): 04384139
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPs) (Pounds/Year)
Pollutant CAS CY 2018 CY 2017 Demini- %
from ED from Fees mus Change
Chromic acid.(VI) (Component of So1CR6 &CRC) 7738-94-5 7.58 7.39 0.01 2.5%
Lead& compounds 22.29 21.75 . 1.0 12.5%
Lead Unlisted Compounds- Specify Compound 'PBC-Other 22.29 21.75 10.0 2.5%
(Component of PBC)
Mercury & Compounds-all total mass includes Hg Vapor 1.11 1.09 0.001 1.8%
Mercury, vapor(Component of HGC) 7439-97-6 1.11 1.09 0.001 2.5%
Nickel& Compounds,sum total mass includes elemental 10.70 10.44 1.0 12.5%
Nickel metal (Component of NIC) 7440-02-0 10.70 10.44 1.0 F2.5%
Polycyclic Organic Matter(Specific Compounds from OAQPS 9.66 9.42 1.0 12.5%
or TP9
Naphthalene (Component of 83329/POMTV) 91-20-3 9.66 9.42 1.0 F2.50/,
Benzene 71-43-2 430.97 420.47 1.0 2.5%
Chlorine 7782-50-5 193.19 188.49 100.0 2.5%
DEHP (Di(2-ethylhexyl)phthalate) 117-81-7 297.22 289.98 10.0 2.5%
Dichlorobenzene(p), 1,4- 106-46-7 7.13 6.96 1.0 2.5%
Ethyl chloride (chloroethane) 75-00-3 84.71 82.64 10.0 2.5%
Fluorides(sum of all fluoride compounds as mass of 16984-48-8 2,377.74 2,319.84 10.0 2.5%
ion)
Formaldehyde 50-00-0 24.51 23.91 10.0 2.5%
Hexane, n- 110-54-3 0.198530 0.198530 100.0 0.0%
Hydrogen chloride (hydrochloric acid) 7647-01-0 4,458.27 4,349.70 100.0 2.5%
Hydrogen fluoride(hydrofluoric acid as mass of HF) 7664-39-3 1,486.09 1,449.90 100.0 2.5%
(Component of 16984488/Fluorides)
Methyl chloride (chloromethane) 74-87-3 99.57 97.14 1.0 2.5%
Methyl iodide (iodomethane) 74-88-4 13.82 13.48 10.0 2.5%
Selenium Compounds SEC 34.18 33.35 10.0 2.5%
Styrene 100-42-5 2.97 2.90 100.0 2.5%
08/28/2019 Page 2 of 3

Facility Total CY 2018 Emission Summary'Recorded in ED Facility ID #: 1900009
Facility Name: General Shale Brick, Inc. -Moncure Facility Permit#(s): 04384T39
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPS) (Pounds/Year)
Pollutant CAS CY 2018 CY 2017 Demini- %
from ED from Fees mus Change
Toluene 108-88-3 23.78 23.20 100.0 2.10
Largest Individual HAP Hydrogen chloride(hydrochloric acid) 4,458.27 lbs
Total HAP Emissions 7,214.78 lbs
Largest Individual CAP CO 84.70 tons
Total CAP Emissions 189.86 tons
Total TAP Emissions 9,323.69 lbs
Total Aggregate 194.12 tons
Emissions
DAO's Comments Regarding Inventory
Brick production for 2018 was up 2.496 percent from the brick production in 2017. Emission factors for hydrogen fluoride,hydroge
chloride,and total fluorides have been corrected to reflect the SSCB approved test results for the Kiln 4 test that took place on
September 24,2015 that established the site specific emission factors for these pollutants. Kiln 4 was the only kiln that operated in
CY 2018. _
08/28/2019 Page 3 of 3

I T11kL
I
.................................................................................................................................................................................................
2018 CALENDAR YEAR EMISSIONS INVENTORY
General Shale Brick, Inc. - Moncure, NC Facility
General Shale Brick
Building The American Dream'
I
NC Dept of Environmental Quality
June 2019
Raleigh Regional Office
Project 193401.0086
I
Prepared By:
TRINITY CONSULTANTS
One Copley Parkway
Suite 205
Morrisville,NC 27560
[phone]
Tinn. i /X
I
y
Consi Cants
IEnvironmental solutions delivered uncommonly well

WoodFuel/Sawdust System(New).............................................................................................................................................16
ClayHandling Equipment................................................................................................................................................................20
IntersiteConveyer.............................................................................................................................................................................21
BrickTexturing..................................................................................................................................................................................23
CoatingsDryer......................................... .............................................................24
VacuumSystem...................................................................................................................................................................................28
StorageTanks i ...................................................................................................................................................................................29
FlyashSilo............................................................................................................................................................................................30
{ Cement Silo..........................................................................................................................................................................................31
1 ;,
BatchMixer..........................................................................................................................................................................................32
Rumbler................................................................................................................................................................................................33
Summaryof Emissions................................. ..................................................................................................................................34
FugitiveSources.................................................................................................................................................................................36
t
i
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General Shale Brick, Inc. -Moncure, NC Facility I CY 2018 Emissions Inventory
Trinity Consultants

SECTION 1
NCDAQ CY 2018 EMISSION INVENTORY (AERO) FORMS
i -
General Shale Brick, Inc.-Nloncure, NC Facility I CY 2018 Emissions Inventory
Trinity Consultants

COPY of RECORD Date Submitted: 6/14/2019 17:27:17
Inventory Certification Form(Title V)
Facility Name: General Shale Brick,Inc.—Moncure Facility Facility ID: 1900009
300 Brick Plant Road Permit• 04384
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 2018
These forms must be completed and returned even if the facility did not ongrgte or nmtcc�n„e
The legally defined "Responsible Official" of record for your facility is Kevin Ham
This person or one that meets the definition below must sign this certification form.
The official submitting the information must certify that he/she complies with the requirements as specified in Title 15A
NCAC 2Q.0520(b)which references and follows the federal definition.40 CFR Part 70.2 defines a responsible as meaning one
of the following:
1. For a corporation:a president, secretary, treasurer,or vice—president of the corporation in charge of a principal
business function,or any other person who performs similar policy or decision making functions for the overall
operation of one or more manufacturing,production,or operating facilities applying for a or subject to a permit and
either
i.the facilities employ more than 250 persons or have gross annual sales or expenditures exceeding$25
million(in second quarter 1980 dollars);or
ii.the delegation of authority to such representatives is approved in advance by the permitting authority;
2. For partnership or sole propietorship;a general partner or the proprietor,respectively;
3.for a muncipality,state,federal,or other public agency includes the chief executive officer having responsibility for the
overall operations of a principal geographic unit of the agency(e.g.,a Regional Administrator of EPA).
CERTIFICATION STATEMENT-
I certify that I am the responsible official for this facility, as described above, and hereby certify that the information contained
in this air emissions report, including attached calculations and documentation, is true,accurate and complete. (Subject to legal
penalities of up to$25,000 per occurrence and possible imprisonment as outlined in G.S.§143-215.3(a)(2))
Responsible Official's Signature Below use blue ink): Date Signed:
Printed Name:�Kev*n Ham
Signature:
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: 6/14/2019 17:27:17 1

COPY of RECORD Date Submitted: 6/14/2019 17:27:17
As entered in AERO
Facility Name: General Shale Brick,Inc.—Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit: 04384
Moncure,NC 27559 County: Chatham
DAQ Region : RRO
Listing of Emission Sources and Control Devices on Permit.-See instructions
ES ID on Air ES Description CS ID CS Description CD ID's
Permit
Batch mixer(39.97 tons per one bagfilter(535 sgaure
ES—BP—BM hour capacity) CS-12 feet of filter area), CD-BP—BH1
ES—BP—CS Cement silo(10 tons per hour CS-13 one bin vent filter(227 CD—BP—BV2
capacity) square feet of filter area),
ES—BP—FAS Flyash silo(I I tons per hour CS-14 one bagfilter(535 sqaure CD—BP—BH1
capacity) feet of filter area),
Natural-.gas—fired rotary drum
ES—CD-8 coatings dryer(250,000 Btu
per hour heat input;3.45 tons
per hour drying capacity)
bagfilter(6,096 square feet
of filter area),Bagfilter(6,096
square feet of filter
ES—CRS Texturizing operation for Line CS-19 area),bagfilter(4,062 square CD—CR6BF,CD—CR7BF1,
I feet of filter area),bagfilter CD—CR7BF2,CD-CR7BF3
(3,040 square feet of filter
area),
bagfilter(6,096 square feet
of filter area),Bagfilter(6,096
Texturizing operation for Line square feet of filter CD—CR6BF,CD—CR7BF 1,
ES—CR6 2 CS-19 area),bagfilter(4,062 square CD—CR7BF2,CD—CR7BF3
feet of filter area),bagfilter
(3,040 square feet of filter
area),
bagfilter(6,096 square feet
of filter area);Bagfilter(6,096
feet of filter
Texturizing operation for squareCD—CR6BF,CD—CR7BF1,
ES—CR7 CS-19 area)bagfilter.(4,062 square
Lines 3 and 4 feet of filter area),bagfilter CD—CR7BF2, CD—CR7BF3
(3,040 square feet of filter
area),
ES—CR8 Texturizing operation for lines
3 and 4
ES—Coal—CC Coal crusher CS-18 bagfilter(air to cloth ration CD—Coal=CC
of 4.7 to 1),
ES—Kl Wood/natural gas—fired tunnel CS-8 Two Simple cyclones(89 CD—C1,CD—C2
brick kiln(20.3 million Btu inches'in diameter)
2

per hour heat input and 13.7
tons per hour fired brick
production rate) [21) .1109
Case By Case MACT]
Wood/natural gas—fired tunnel
brick kiln(20.3 million Btu
ES—K2 per hour heat input and 13.7 CS-8 Two Simple cyclones(89 CD—CI, CD—C2
tons per hour fired brick inches in diameter)
production rate)[2D .1109
Case By Case MACT]
Natural gas/propane—fired
ES_—K3D1 brick dryer(4.43 million Btu
per hour heat input)
Natural gas/propane—fired
ES—K3D2 brick dryer(4.43 million Btu
per hour heat input)
- Natural gas/propane—fired
ES—K3D3 brick dryer(4.43 million Btu
per hour heat input)
POS—Natural
gas/propane—fired brick tunnel
kiln(25.9.million Btu per hour
heat input and 20.55 tons per
hour maximum fired brick
production rate) [21) .1109
ES—K3K Case By Case MACT]AOS—Coal/NaturalCS-15 dry limestone adsorber, CD—K3DLA
gas/propane—fired brick tunnel
kiln(25.9 million Btu per hour
heat input and 20.55 tons per
_n
hour maximum fired brick
production rate) [21).1109
Case By Case MACT]
Natural gas/propane—fired
ES—K4D 1 brick dryer(4.43 million Btu
per hour heat input)
Natural gas/propane—fired
ES—K4D2 brick dryer(4.43 million Btu
per hour heat input)
Natural gas/propane—fired
ES—K4D3 brick dryer(4.43 million Btu
per hour heat input)
ES—K4K POS—Natural CS-11 dry limestone adsorber, CD—K4DLA
gas/propane—fired brick tunnel
kiln(25.9 million Btu per hour
heat input and 20.55 tons per
hour maximum fired brick
production rate)[21).1109
Case By Case MACT]AOS—
Coal/natural
gas/propane—fired brick tunnel
kiln(25.9 million Btu per hour
3

heat input and 20.55 tons per
hour maximum fired brick
production rate)[21).1109
Case By Case MACT]
ES—RUMBLE Rumbler system
ES—SS Sand silo storage
One rotary sawdust dryer
(5.59 tons per hour drying
= ES—WD1,2 capacity;heated by recycle CS-8 Two Simple cyclones (89
heat from kilns 1 and 2 with inches in diameter) CD-C1,CD—C2
- natural gas used as a
supplemental fuel)
dust collector(air to cloth
ratio of 8.17 to 1),dust
collector(air to cloth ratio of
8.06 to 1),cyclone(42 inches CD—SD—DC I,CD—SD—DC2,
ES—WFS—SD—CV1 Transfer screw conveyor CS-17 CD—WFS—SD—CYC,
- in diameter),bin vent filter(air CD—SD—BV 1,CD—SD—BV2
to cloth ratio of 4.44 to 1),bin
vent filter(air to cloth ratio of
4.44 to 1),
dust collector(air to cloth
ratio of 8.17 to 1-),dust
-- collector(air to cloth ratio of CD—SD—DC1,CD—SD—DC2,
ES—WFS—SD—CV2 Screen feed screw conveyorCS-17 8.06 to 1),cyclone(42 inches
CD—WFS—SD—CYC,
in diameter),bin vent filter(air CD—SD—BV1,CD—SD—BV2
to cloth ratio of4.44.to 1),bin
vent filter(air to cloth ratio of
4.44 to 1),
dust collector(air to cloth
ratio of 8.17 to 1),dust
collector(air to cloth ratio of CD—SD—DC I,CD—SD—DC2,
in di
ES—WFS—SD—CV3 Enclosed conveyorCS-17 to 1),cyc inches
- n diameter),bin
e n vent
filter(air CD—WFS—SD=CYC,
to cloth ratio of 4.44 to 1),bin CD—SD—BV1,CD—SD—BV2
vent filter(air to cloth ratio of
4.44 to 1),
dust collector(air to cloth
ratio of 8.17 to 1),dust
collector(air to cloth ratio of CD—SD—DC I,CD—SD—DC2,
ES—WFS—SD—CYC.Cyclone CS-17 8.06 to 1),cyclone(42 inches
Y in diameter),bin vent filter(air CD—WFS—SD—CYC,
to cloth ratio of 4.44 to 1),bin CD—SD—BV1,CD—SD—BV2
vent filter(air to cloth ratio of
4.44 to 1),
dust collector(air to cloth.
ratio of 8.17 to 1),dust
collector(air to cloth ratio of
806 to 1),cyclone(42 inches CD—SD—DC I,CD—SD—DC2,
.
ES—WFS—SD—HM Hammermill CS-17 CD—WFS—SD—CYC,
in diameter),bin vent filter(air
to cloth ratio of 4.44 to 1),bin CD—SD—BV1,CD—SD—BV2
vent filter(air to cloth ratio of
4.44 to 1),
4

dust collector(air to cloth
_ ratio of 8.17 to 1),dust
collector(air to cloth ratio of8. CD—SD—DC I,CD—SD—DC2,
ES—WFS—SD-SC1 8x8 screen CS-17 in di to 1),cyclone e vent n inches CD—WFS—SD—CYC,
n ameter),bit filter(air CD—SD—BVI,CD—SD—BV2
to cloth ratio of 4.44 to 1),bin
vent filter(air to cloth ratio of
4.44 to 1),
dust collector(air to cloth
ratio of 8.17 to 1),dust
collector(air to cloth ratio of CD—SD—DC1,CD—SD—DC2,
ES—WFS—SD—SC2 8x8 screen CS-17 8.06 to 1),cyclone e vent
inches CD—WFS—SD—CYC,
-_ in diameter),bi vent filter(air CD—SD—BV1,CD—SD—BV2
to cloth ratio of 4.44 to 1),bin
vent filter(air to cloth ratio of
4.44 to 1),
dust collector(air to cloth
ratio of 8.17 to 1),dust
collector(air to cloth ratio of CD—SD—DC I,CD—SD—DC2,
ES—WFS—SD—SDS Sawdust silo CS-17 8.06 to 1),cyclone(42 inches CD—WFS—SD—CYC,
in diameter),bin vent filter(air CD—SD—BVI,CD—SD—BV2
to cloth ratio of 4.44 to 1),bin
vent filter(air to cloth ratio of
4.44 to 1),
dust collector(air to cloth
ratio of 8.17 to 1),dust
collector(air'to cloth ratio of CD—SD—DCl,CD—SD—DC2,
ES—WFS—SD—SH Surge hopper CS-17 8.06 to 1),cyclone(42 inches CD—WFS—SD—CYC,
in diameter),bin vent filter(air CD—SD—BVI,CD—SD—BV2
to cloth ratio of 4.44 to 1),bin
vent filter(air to cloth ratio of
4.44 to 1),
F—C—CFBH Intersite conveyor[NSPS
000]
F—CH—BC Brickhaven conveyor[NSPS
000]
F—CH—Cl One impact crusher[NSPS
000]
F—CH—CFC Cape Fear conveyor[NSPS
000]
F—CH—FC Feed conveyor[NSPS 000]
F—CH—FS 1 Finishing screen[NSPS 0001
F—CH—FS2 Finishing screen[NSPS 000]
F—CH—FS3 Finishing Screen[NSPS
000]
F—CH—FS4 Finishing screen [NSPS 000]
F—CH—HI Hammermill [NSPS 000]
F—CH-112 Hammermill[NSPS 000]
F—CH—HFC I Hammermill Feed Conveyor
[NSPS 000]
5

Hammermill Feed Conveyor
F—CH—HFC2 y
[NSPS 000]
F—CH—PI Product conveyor[NSPS
000]
F—CH—P2 Product conveyor[NSPS
000]
F—CH—RC Reversing conveyor[NSPS
000]
- F—CH—SFC1 Screen feed conveyor[NSPS
000]
F—CH—SFC2 Screen feed conveyor[NSPS
000]
F—CH—SFC3 Screen feed conveyor[NSPS
000]
F—CH—SFC4 Screen feed conveyor[NSPS
000]
F—CH—SS1 Scalping screen [NSPS 000]
F—CH—SS2 Scalping Screen[NSPS 000]
F—CH—SSFC Scalping conveyor[NSPS
000]
F—CH—T1 Tailings conveyor[NSPS
000]
F—CH—T2 Tailings conveyor[NSPS
000]
F—CH—TC1 Trampolin Conveyor[NSPS
000]
F—CH—TC2 Trampolin Conveyor[NSPS
000]
F—FC4 Finishing conveyor#4[NSPS
000]
F—FC5 Finishing conveyor#5 [NSPS
000]
F—FS1 Single deck screen[NSPS
000]
F—FS2 Single deck finishing screen
[NSPS Subpart 000]
F—FS3 Finishing screen[NSPS 000]
F—FS4 Finishing screen[NSPS 000]
F—FSS Finishing screen
F—FS6 Finishing screen
F—FS7 Finishing screen
F—FS8 Finishing screen
F—FS9 Finishing Screen
F—PC Primary crusher[NSPS 000]
F—SGS Secondary crusher[NSPS
000] .
F—SS1 Scalping Screen[NSPS 000]
6

F—SS2 Scalping Screen[NSPS 000]
I—ES—K1D1 brick dryer associated with
Kiln I
I—ES—K2D I brick dryer associated with
- Kiln 2
I—F—CH—AF Apron feeder
I—F—CH—H Hopper(50 ton capacity)
I—F—Coal--CH Coal hopper
I—F—Coal—CP Coal pile
I—F-SSC Sand Conveyor
IES—CP Open clay storage piles
Existing raw material
IES—F—CH6 handling and conveying
operations
IES—F—CO-2 Reclaimer(coating
operations)
IES—F—CO—C1 Conveyor(coating operation)
IES—F—CO—C2 Conveyor(coating operation)
IES—F—CO—C3 Conveyor(Coating operation)
IES—F—CO—C4 Conveyor(Coating operation)
IES—F—CO—CS Conveyor(coating operation) )
IES—K4F.1 Box feeder for Line_4
IES—K4F.2 conveying system for line 4
IES—K4F.3 storage tank for line 4
IES—RECLAIM Reclaimer building storage
piles
Wood receiving,
IES—SD non—pneumatic handling and
conveying and storage
operations
IES7T1 350 gallon brick oil tank
IES—T2 350 gallon gear oil tank
IES—T3 275 gallon waste oil tank
IES—T4 1,000 gallon diesel tank
IES—T5 1,000 gallon gasoline storage
- tank
Package—type kiln car Two Bagfilters(97 square
IES—VS1 CS-10 feet and 297 square feet of CD—VS1,CD—VS2
vacuuming system
filter area)
Package—type kiln car Two Bagfilters(97 square
IES—VS2 CS-10 feet and 297 square feet of CD-VS1,CD—VS2
vacuuming system
filter area) .
IES—VS3 Hi—Vac vacuum system for
Kiln 3
IES—VS4 package—type kiln car
vacuuming system
IES—VS5
7

package—type kiln car
vacuuming system
IF—BH—MR—C One Conveyor at Brickhaven
site
IF—BH—MR—DH One dump hopper at
Brickhaven site
Screened Clay Conveying and
IS-3 Handling Operation for Kiln 1
and 2
Screened clay conveying and
IS-4 handling operation for Kiln 3
and 4
IS-7.1 Sand coating pile
IS-7.2 Sand coating pile
IS-7.3 Sand coating pile
- IS-7.4 Sand coating pile
IS-7.5 Sand coating pile
IS-7.6 Sand coating pile
IS-7.7 Conveyor
IS-7.8 Conveyor
IS-8.1 Kiln 3 storage pile
IS-8.2 Kiln 3 box feeder
IS-8.3 Kiln 3 storage bin
IS-8.4 Kiln 3 conveyor
IS-8.5 Kiln 3 conveyor
IS-8.6 Kiln 3 conveyor
IS-8.7 Kiln 3 conveyor
IS-8.8 Kiln 3 conveyor
IS-8.9 IKiln 3 conveyor
' I
8

I
COPY of RECORD Date Submitted: 6/14/2019 17:27:17
-; As entered in AERO
f
Facility Name: General Shale Brick,Inc. -Moncure Facility _ Facility ID : 1900009
300 Brick Plant Road Permit : 04384
Moncure,NC 27559 County : Chatham
DAQ Region :RRO
Emission Source & Operating Scenario List- See Instructions
ES Group ID ES ID OS 11) . OS Description
GR12 ES-K3D1,ES-K3D2,ES-K3D3 20 Natural gas/propane-fired dryers
l
for Kiln 3
ES-WFS-SD-CVI,ES-WFS-SD-CV2,
ES-WFS-SD-CV3,ES-WFS-SD-CYC,
GR21 ES-WFS-SD-HM,ES-WFS-SD-SC1, 30 Wood Fuel/Sawdust System
ES-WFS-SD-SC2,ES-WFS-SD-SDS,
ES-WFS-SD-SH
GR22 IES-VS3,IES-VS4,IES-VS5 35 Vacuum Systems-Brickhaven
1'
G-66 ES-K1,ES-K2,ES-WD 1,2 14 Wood/natural gas-fired brick kilns
and green brick dryer(Cape Fear)
G-69 ES-CRS,ES-CR6,ES-CR7 37 Texturizing Operations
G-70 IES-VS1,IES-VS2 34 Vacuum System
F-C-CFBH,F-FC4,F-FCS,F-FSI,
F-FS2,F-FS3,F-FS4,F-FSS,F-FS6, Primary Clay Grinding and
G-71 F-FS7,F-FS8,F-FS9,F-PC,F-SS1, 31 Screening Operation
F-SS2
G-72 I-ES-K1D1,I-ES-K2DI IS Dryers associated with Kilns 1 and
2
( F-CH-BC,F-CH-C1,F-CH-CFC,
F.-CH-FC,F-CH-FSI,F-CH-FS2,
-` F-CH-FS3,F-CH-FS4,F-CH-HI,
f F-CH-H2,F-CH-HFCI,F-CH-HFC2,
- G-132 F-CH-P1,F-CH-P2,F-CH-RC, NONE NONE
F-CH-SFCI,F-CH-SFC2,F-CH-SFC3,
I F-CH-SFC4,F-CH-SS1,F-CH-SS2,
F-CH-SSFC,F-CH-T1,F-CH-T2,
F-CH-TC I,F-CH-TC2
G-135 ES-K4D1,ES=K4D2,ES.-K4D3 29 Natural gas/propane-fired dryers
- for Kiln 4
G-143 I-F-CH-AF,I-F-CH-H,IES-CP, NONE NONE
IES-F-CH6,IES-F-0072,
-' IES-F-CO-C1,IES-F-CO-C2,
IES-F-CO-C3,IES.F-CO-C4,
IES-F-CO-CS,IES-K4F.1,IES-K4F.2,
- IES-K4F.3,IES-RECLAIM,
_ IF-BH-MR-C,IF-BH-MR-DH,IS-3,
IS-4,IS-7.1,IS-7.2,.IS-7.3,IS-7.4,
IS-7.5,.IS-7.6,IS-7.7,IS-7.8,IS-8.1,
1 _ 9

—I - IS-8.2,IS-8.3,IS-8.4,IS-8.5,IS-8.6,
IS-8.7,IS-8.8,IS-8.9
-- G-144 IES—T1,IES—T2,IES—T3,IES—T4,
IES—T5 18 Storage tanks
ES—BP—BM 26 Batch Mixer
ES—BP—CS 27 Cement Silo
ES—BP—FAS 28 Fly ash Silo
' Rotary sand drum dryer(3.45 tons
ES—CD-8 6
per hour)
ES—CR8 NONE NONE
j ES—Coal—CC 33 Coal Processing System'
Natural gas/propane—fired kiln#3
ES—K3K 10 (Uncontrolled)
25
10/Natural gas/propane/coal—fired
kiln#3
ES—K4K 21 Coal/Natural gas/Propane—fired
! kiln#4
ES—RUMBLE 36 Rumbler tumbles blocks in a
rotating drum in order to create an
�- ES—SS NONE NONE
F—SGS NONE NONE
I—F—Coal—CH NONE NONE
I—F—Coal—CP NONE NONE
I—F—SSC NONE NONE
IES—S-D NONE NONE -
f
4 -
V
10

COPY of RECORD Date Submitted: 6/14/2019 17:27:17
i
As entered in AERO
Facility Name: General Shale Brick,Inc. —Moncure Facility Facility ID: 1900009
- 300 Brick Plant Road Permit: 04384
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 2018
1. Emission Source ID(from permit)or . Group GR12 consisting of ES—K3D1,E8—K3D2,ES—K3D3
Emission Source Group ID
2. Emission Source Description: Natural gas/propane—fired dryers at Brickhaven Plant
3. Operating Scenario ID/Description: OS—20/Natural gas/propane—fired dryers for Kiln 3
4. SCC Number/Description: 30500351/Brick Manufacture—Dryer;Brick Dryer: Heated With Waste Heat
And Supplemental Gas Burners
r -
5. Throughput/units in 2018:
-(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
Btu/units
7. `Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. ;Control Device Information :None
'Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
(in 0.1 feet)
- ERP for ES—K3K,
EP—K3 VERTICAL STACK 35 4.92 .99.95 33.79 38544.24 ES—K3D1 AND
ES—K3D2
- 11

Operating Scenario: OS—20 Emission Source/Group ID: GR12
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2018)
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% ine—Aug. 25% Sept.—Nov. 25%
018 �arch—May
18 018 018
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
2018
Criteria Emissions— Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission
Code Pollutants Method Code (Net after Factor Ef Control
Pollutants -
(Tons/Year) (See Instructions) all controls) ,
r 2018
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02. S02 08
VOC VOC 08
HAPITAP 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
2018
I
} 12

(� l �v-Z OPtct -ram
COPY of RECORD Date Submitted: 6/14/2019 17:27:17
As entered in AERO
Facility Name: General Shale Brick,Inc.—Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit: 04384
_ Moncure,NC 27559 Counh,:.Chatham
DAQ Region,,: RRO
_ North Carolina Department of Environment and Natural Resources
Division of Air Quality -
Air Pollutant Point Source Emissions Inventory—Calendar Year 2018
I. Emission Source ID(from permit)or Group GR21 consisting of ES—WFS—SD—CV 1,ES—WFS—SD—CV2,
Emission Source Group ID ES—WFS—SD—CV3,ES—WFS—SD—CYC,ES—WFS—SD—HM,
ES—WFS—SD—SC1,ES—WFS—SD—SC2,ES—WFS—SD=SDS,
ES—WFS—SD—SH
2. Emission Source Description: Wood Fuel/Sawdust System
3. Operating Scenario ID/Description: OS—30/Wood Fuel/Sawdust System
4. SCC Number/Description: 30500305Brick Manufacture—Material Prep ;Raw Material Handling and
Transferring
5. Throughput/units in 2018:
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) r
Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information
Order CS—ID' CD H) Control Device Description
as listed in permit)
1 CS-17 CD—SD—DC1 Dust collector 8.71:1 air to cloth ratio
2 CS-17 CD—SD—DC2 Dust collector 8.06:1 air to cloth ratio
3 CS-17 CD—WFS—SD—CYC Cyclone. 42 inches in diameter
4 CS-17 CD—SD-BV1 One bin went filter 4.44:1 air to cloth ratio
I 5 CS-17 CD—SD—BV2 One bin vent.filter 4.44:1 air to cloth ratio
f
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)
1
13

P SD—BV 1 VERTICAL STACK 20 0.5 72 33.95 400 Bin vent on sawdustsilo
Dust Collector on
P—SD—DC2 VERTICAL STACK 20 1 72 49.76 2345 Woodfuel Sawdust
System Screens
Conveyors
P—SD—BV2 VERTICAL STACK 20 0.5 75 33.95 400 Bin Vent on Surge
Hopper
_}
Dust Collector on
P—SD—DC1 VERTICAL STACK 20 1 72 44.56 2100 Woodfuel Sawdust
System Screens
i
Conveyors
I
i
14

- Operating Scenario: OS—30 Emission Source/Group ID:GR21
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2018)
Hours per Da 24 Days per Week 7 Weeks per Year 52
' P Y ( ) Y P ( ) P ( )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
r01an--Feb8 +Dec 250�o arch—May 250�oune—Aug. 250�o �018
ept.—Nov. 25%
018 �018
13. Actual Emissions per Pollutant Listed
it
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
2018
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)
2018
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
j PM2.5 PM2.5 08
S02 S02 08
VOC, VOC 08
HAP/TAP CAS Emissions Emission Control
Pollutants (In HAP/TAPS Estimation Emission EF Control
- (see instructions) Efficiency
Alphabetical Order) (Pounds/Year) Method Code (Net after all controls) Factor
See Instructions
2018
i
15

COPY of RECORD Date Submitted: 6/14/2019 17:27:17
-- As entered in AERO
Facility Name: General Shale Brick,Inc.—Moncure Facility Facility ID : 1900009
-- 300 Brick Plant Road Permit: 04384
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 2018
1. Emission Source ID (from permit)or Group GR22 consisting of IES—VS3,IES—VS4,IES—VS5
Emission Source Group ID
2. Emission Source Description: Vacuum Systems—Brickhaven
3. Operating Scenario ID/Description: OS—35/Vacuum Systems—Brickhaven
4. SCC Number/Description: 30500317Brick Manufacture—Material Prep ;Raw Material Unloading
v
5. Throughput/units in 2018: 2000 HR/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
(Btu/units)
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
l
8. Control.Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point(E
RP) Information: Sources vented to more than one ERP use additional e tKy 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
)
in 0.I feet)
EP—VS3 DOWNWARD—FACING VENT I 3 72 3.3 1400 Emission Point for
IES—VS3
EP—VS4 DOWNWARD—FACING VENT 1 3 72 3.3E 1400 Emissions point
- for IES—VS4
EP—VS5 DOWNWARD—FACING VENT 1 3 72 3.3 1400 Emission point for
� IES—VS5
is
16

Operating Scenario: OS—35 Emission Source/Group ID: GR22
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2018)
--' 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% 018
25% une—Aug. 25% Sept.—Nov. 25%
018 018 018 018
13. Actual Emissions per Pollutant Listed
I '
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
i Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
. 2018
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency
Emission
��QS Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
j 2018
CO CO 08
NOx NOx 08 .
TSP TSP 0.12 08
PM10 PM10 0.12 08
i
PM2.5 PM2.5 0.12 08
S02 S02 08
VOC VOC 08
HAP/TAP Emissions Emission
CAS Estimation Control Emission
Pollutants (In (see instructions) HAP/TAPS Method Code Efficiency Factor EF Control
_ Alphabetical Order) (Pounds/Year) structions (Net after all controls)
See In
2018
s
j 17

a/
J Lio No--r ®PF�-rG
COPY of RECORD Date Submitted: 6/14/2019 17:27:17
As entered in AERO
Facility Name: General Shale Brick,Inc. —Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit : 04384
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 2018
I� 1. Emission Source ID(from permit)or Group G-66 consisting of ES—K1,ES—K2,ES—WDI,2
Emission Source Group ID
2. Emission Source Description: Two Wood/natural gas—fired brick kilns and green brick dryer
3. Operating Scenario ID/Description: OS— 14/Wood/natural gas—fired brick kilns and green brick dryer(Cape Fear)
4. SCC Number/Description: 30500361Brick Manufacture—Dryer; Sawdust Dryer:Heated With Exhaust
From Sawdust—fired Kiln
' 5. Throughput/units in 2018:
(e.g.production or fuel use):
it
6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-8 CD—CI Simple cyclone 89 inches in diameter
f 2 CS-8 CD—C2 Simple cyclone 89 inches in diameter
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/see) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
ERP for ES—KI,
EP—CI VERTICAL STACK 65 2.5 150 53 15609.78 ES-K2,and
ES—SDI
ERP for ES—K1,
EP—C2 VERTICAL STACK 65 2.5 150 53 15609.78 ES—K2,and
ES—SDI
18

Operating Scenario:OS— 14 Emission Source/Group ID: G-66
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2018)
- 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 250�o une—Aug. 25% Sept.—Nov. 25%
018 018 )18 018
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
2018
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)
2018
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP Emissions Emission Control
CAS HAP/TAPS Estimation Emission
Pollutants (In Efficiency
(see instructions) Method Code Factor EF Control
_- Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
1 -
2018
-1
20

COPY of RECORD Date Submitted: 6/14/2019 17:27:17
As entered in AFRO
Facility Name: General Shale Brick,Inc.—Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit: 04384
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 2018
1. Emission Source ID (from permit)or Group G-69 consisting of ES—CR5,ES—CR6,ES—CR7
_ Emission Source Group ID
2. Emission Source Description: Texturizing Operations
3. Operating Scenario ID/Description: OS—37/Texturizing-Operations
4. SCC Number/Description: 30500397Brick Manufacture; *Other Not Classified
5. Throughput/units in 2018: 148609 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, 100
Device or Stack):
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed in ermit
1 CS-19 CD—CR6BF ba filter 6,096 square feet of filter area
2 CS-19 CD—CR7BF1 Ba filter 6,096 square feet of filter area
3 CS-19 CD—CR713172 ba filter 4,062 square.feet of filter area
4 CS-19 CD—CR7BF3 ba filter 3,040 square feet of filter area
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional e try lines):
ERP ID ERP Type Height .Diameter Temperature Velocity Volume Flow ERP Description
- (in feet) Circle(enter ft (F) (Feet/see) Rate(Acfm)
Rectangle(L x W)
in.0.1 feet)
EP—CR6 HORIZONTAL TACKI 20 1 1 72 21.2 999.02 ERP for ES—CR-6
EP—CR7 1HORIZONTAL STACKI 20 1 1 1 72 1 21.2 1 999.02 ERP for ES—CR-7
21

Operating Scenario: OS—37 Emission Source/Group ID: G-69
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2018)
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%° nne—Aug. 25% Sept.—Nov. 25%
018 018 018 018
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
- GHG CAS GHG Estimation Efficiency Emission
Pollutants Pollutants Method Code (Net after Factor Ef Control
Tons/Year See Instructions all controls
2018
z
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Dunss Code Pollutants Method Code (Net after Factor Ef Control
Pollutant (Tons/Year) (See Instructions) all controls)
2018
CO CO 08 0
NOx NOx 08 0
TSP TSP 0.27 08 ; 99 0.0036 AFTER
PM10 PM10 0.27 08 99 0.0036 AFTER
PM2.5 PM2.5 0.27 08 99 0.0036 AFTER
S02 S02 08 0
VOC VOC 08 0
HAP/TAP CAS Emissions Emission
Control
Pollutants (In. HAP/TAPS Estimation Emission
Method Code Efficient Factor EF Control .
(see instructions) Y
. Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2018
22

COPY of RECORD Date Submitted: 6/14/2019 17:27:17
' As entered in AERO
Facility Name: General Shale Brick,Inc.—Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit: 04384
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 2018
1. Emission Source ID(from permit)or Group G-70 consisting of IES—VS1,IES—VS2
Emission Source Group ID
2. Emission-Source Description: Vacuum System
3. Operating Scenario ID/Description: OS—34/Vacuum System
4. SCC Number/Description: 30500317/Brick Manufacture—Material Prep;Raw Material Unloading
5.. Throughput/units in 2018: 1500 HR/yr
(e.g.production or fuel use):
6. Fuel Informatio_n (If fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-10 CD—VS1 Ba filter 97 square feet of filter area
- 2 CS-10 CD—VS2 Ba filter 297 square feet of filter area
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entr-y lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm) Description
Rectangle(L x
)
in 0.1 feet)
EPVS2 DOWNWARD—FACING VENT 1 3 72 3.3 1400 ERP for
CD—VS2
EP.VS1 DOWNWARD—FACING VENT 1 3 72 3.3 1400 ERP for
- CD-V S 1
23

_ Operating Scenario: OS—34 Emission Source/Group ID:G-70
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2018)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
i� 11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
—i an—Feb +Dec arch—Ma
25% 0 r y 25% une—Aug. 25% Sept.—Nov. 25%
018 018 21
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
-- GHG CAS GHG Estimation Efficiency Emission
Pollutants Pollutants Method Code (Net after Factor Ef Control
Tons/Year See Instructions all controls
2018
7 Criteria Emissions— Emission Control
Pollutant Criteria Estimation
Efficiency Emission(NAAQS)
Code
Pollutants Pollutants Method Code (Net after Factor Ef Control
(Tons/Year) (See Instructions) all controls)
2018
CO CO 08 0
—i NOx NOx' 08 0
I .
TSP TSP 0.09 08 99.9 AFTER
PM10 PM10 0.09 08 99.9 AFTER
PM2.5 PM2.5 0.09 08 99.9 AFTER
S02 S02 Og 0
VOC VOC 08 0
HAP/TAP Emissions Emission Control CAS
Pollutants (In. HAP/TAPSEstimation Emission
Al habetical Order (see instructions) Method Code Efficiency Factor EF Control
P ) (Pounds/Year) (Net after all controls)
See Instructions
2018
i
24

COPY of RECORD Date Submitted: 6/14/2019 17:27:17
As entered in AERO
Facility Name: General Shale Brick,Inc.—Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit: 04384
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 2018
1. Emission Source ID(from permit)or Group G-71 consisting of F—C—CFBH,F—FC4,F—FC5,F—FS1,F—FS2,
-- Emission Source Group ID F—FS3,F—FS4,F—FS5,F—FS6,F—FS7,F—FS8,F—FS9,F—PC,F—SS1,F—SS2
2. Emission Source Description: Clay Handling Equipment
3. Operating Scenario ID/Description: OS—31/Primary Clay Grinding and Screening Operation
4. SCC Number/Description: 30500302Brick Manufacture—Material Prep;Raw Material Grinding
Screening
5. Throughput/units in 2018: 283360 TON/yr
--` (e.g.production or!fuel use):
6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information':None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9:Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate . ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
EP. FG . FUGITIVE(NO l 72 Area= 1 ERP for Fugitive
STACK) sources
25

Operating Scenario: OS—31 Emission Source/Group ID:G-71
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2018)
Hours per Day ( 6 ) Days per Week ( 5 ) Weeks per Year ( 48 )
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 arch—May 25"�u une—Aug. 25"�u ept.—Nov. 25%
018 018 018 018
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
2018
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAAQS) enc y Ef Control
Pollutants Code Pollutants Method Code (Net after Factor
(Tons/Year) (See Instructions) all controls)
2018
CO CO 08
NOx NOx 08
TSP TSP 3.5-4 6q 08 0.02604
PM10 PM10 0i2'4o 08 0.002$41
PM2.5 PM2.5 0.33 a64 08 0.0023-14
S02 S02 08
VOC VOC 08
HAP/TAP CAS Emissions Emission Estimation Control Emission
Pollutants (In (see instructions) Method Code HAP/TAPS Efficiency E1,' ('ontrol
Alphabetical Order) (Pounds/Year) (Net after all controls) Factor
See Instructions
2018
26

p 1 D [40� O PeA4"r
COPY of RECORD Date Submitted: 6/14/2019 17:27:17
As entered in AERO
Facility Name: General Shale Brick,Inc.—Moncure Facility Facility ID : 1900009
- 300 Brick Plant Road Permit: 04384
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 2018
1. Emission Source ID(from permit)or Group-G-72 consisting of I—ES—K1D1,I—ES—K2D1
Emission Source Group ID
2. Emission Source Description: Dryers associated with materials handling equipment
3. Operating Scenario ID/Description: OS— 15/Dryers associated with Kilns 1 and 2
4. SCC Number/Description: 30500305Brick Manufacture—Material Prep ;Raw Material Handling and
Transferring
5. Throughput/units in 2018:
(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 1D ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter ft (F) (Feet/see) (Acfm)
Rectangle(L x W)
(in 0.1 feet)
EP—FG FUGITIVE(NO 1 72 Area=1 ERP for Fugitive
i
STACK) sources
i
�+ 27

_ Operating Scenario: OS- 15
P g Emission Source/Group ID: G-72
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2018)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&.End Times For Operating Scenario: Start: 0 End: 2359
I
12. Seasonal Periods Percent Annual Throu h ut:
ran--Feb +Dec 250�o arch-May , 250�o une-Aug. 250�o �018
ept.-Nov. 25%
8 �018 �018
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
I
Emissions- Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
i -
2018
f
Criteria Emissions- Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission
Pollutants Code Pollutants Method Code (Net after Factor Ef Control
(Tons/Year) (See Instructions) all controls)
2018
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 Method Estimation Emission
(see instructions) Efficiency EF Control
P ) (Pounds/Year)
Alphabetical Order Code (Net after all controls) Factor
See Instructions
2018
i
28

COPY of RECORD Date Submitted: 6/14/201917:27:17
- As entered in AERO
Facility Name: General Shale Brick,Inc. -Moncure Facility Facility ID : 1900009
- ` 300 Brick Plant Road Permit: 04384
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 2018
1. Emission Source ID(from permit)or Group G-135 consisting of ES-K4D1,ES-K4D2,ES-K4D3
Emission Source Group ID
2. Emission Source Description: Natural gas/propane-fired dryers at Brickhaven Plant
3. Operating Scenario ID/Description: OS-29/Natural gas/propane-fired dryers for-Kiln 4
4. SCC Number/Description: 30500351/Brick Manufacture-Dryer;Brick Dryer:Heated With Waste Heat
jAnd Supplemental Gas Burners
5. Throughput/units in 2018: 148609 TON/yr
"- (e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
l 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 i Information: Sources vented to more than one ERP use additional ntry lines):
ERP 1D 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)
EP-K4D1 VERTICAL STACK 34.78 4.92 99.95 33.79 38544.24 Brick Dryers on
Kiln 4
I �
29

� i
Operating Scenario: OS—29 Emission Source/Group ID: G-135
j. 10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2018)
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 250�o une—Aug. 25"�u Sept.—Nov. 25%
018 018 018 018
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
2018
Criteria Emissions— Emission Control
Criteria Estimation Efficiency Emission Ef Control
I--' (NAA Pollutant Code Pollutants Method Code (Net after Factor
Pollutants (Tons/Year) (See Instructions) all controls)
2018
CO CO 23.03 08 0.31
NOx NOx 7.28 08 0.098
TSP TSP 13.89 08 0.187
PM10 PM10 13.89 08 0.187
PM2.5 PM2.5 13.89 08 0.187
-S02 S02 08
VOC VOC 2.23 08 0.03
HAP/TAP CAS Emissions Emission Control
' Estimation Emission
Pollutants (in (see instructions) HAP/TAPS Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) See Instructions) (Net after all controls)
2018
30

_ 1
COPY of RECORD Date Submitted: 6/14/2019 17:27:17
As entered in AERO
Facility Name: General Shale Brick,Inc.—Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit: 04384
_ Moncure,NC 27559 County : Chatham
DAQ Region :RRO
North Carolina Department of Environment and Natural Resources
j Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2018 .
1. Emission Source ID(from permit)or Group G-144 consisting of IES—T1,IES—T2,IES—T3,IES—T4,IES—T5
Emission Source Group ID
2. Emission Source Description: Storage tanks
3. Operating Scenario ID/Description: OS— 18/Storage tanks
4. SCC Number/Description: 39090004/Fuel Storage—Fixed Roof Tanks;Distillate Oil(No.2):Working
Loss
5. Throughput/units in 2018: 81935 GAL/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
i
j
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) (Feettsec) (Acfm)
Rectangle(L x W)
in 0.1 feet) .
EP—FG FUGITIVE(NO 1 72 Area= I ERP for Fugitive
STACK) sources
�� 31

I i
Operating Scenario: OS— 18 Emission Source/Group ID: G-144
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2018)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
j 11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
II
12. Seasonal Periods Percent Annual Throu h ut:
ran--Feb +Dec 250�o 25% une—Aug. 25"�o �018
ept.—Nov. _F 258 - �arch—May
18 1018
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
I
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission
Pollutants Pollutants Method Code (Net after Factor Ef Control
Tons/Year See Instructions all controls
2018
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficient Emission
(NAAQS) Code y Ef Control
Pollutants Pollutants Method Code (Net after Factor
(Tons/Year) (See Instructions) all controls)
2018
CO CO 08
NOx- ` NOx 08
TSP TSP 08
PM10 PM10 08-
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 0.67 08 0.01638
HAP/TAP CAS Emissions Emission
Control
Pollutants (In HAP/TAPS Estimation Emission
(see instructions)
Efficiency EF Control
Alphabetical Order) (Pounds/Yeaz Method Code
) (Net after all controls) Factor
See Instructions
2018
1
32

COPY of RECORD Date Submitted: 6/14/2019 17:27:17
As entered in AERO
Facility Name: General Shale Brick,Inc.—Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit• 04384
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 2018
1. Emission Source ID (from permit)or ES—BP—BM
Emission Source Group ID
2. Emission Source Description: Batch mixer(39.97 tons per hour capacity)
3. Operating Scenario ID/Description: OS—26Batch Mixer
4. SCC Number/Description: 31299999/Miscellaneous Machinery;Other Not Classified
5. Throughput/units in 2018:
(e.g.production or fuel use):
✓ 6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed inpermit) -
1 CS-12 CD—BP—BHI One ba filter 535 s aure feet of filter area
-9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity .Volume Flow ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
BMX VERTICAL STACK 44.95 1.312 72.05 40.02 3246.27 Batch Mixer
Ba house
33

- Operating Scenario: OS—26 Emission Source/Group ID:ES—BP—BM
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2018)
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% 250�o une—Aug. 25% Sept.—Nov. 25%
018 �arch—May
18 018 018
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
2018
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency
Emission
-- (NAA Code Pollutants Method Code (Net arter Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2018
CO CO 08
NOx NOx 08
TSP TSP 08
PM16 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP CAS Emissions Emission Control
Pollutants (In HAP/TAPS Estimation Emission EF Control
(see instructions) Efficiency
Alphabetical Order Pounds/Year Method Code
p ) ( ) (Net.after all controls) Factor
See Instructions
- 2018
34

COPY of RECORD Date Submitted: 6/14/2019 17:27:17
As entered in HERO .
Facility Name: General Shale Brick,Inc.—Moncure Facility Facility.ID : 1900009
300 Brick Plant Road Permit : 04384
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 2018
I
11. Emission Source ID(from permit)or ES—BP—CS
Emission Source Group ID
2. Emission Source Description: Cement silo(10 tons per hour capacity)
3. Operating Scenario ID/Description: OS—27/Cement Silo
4. SCC Number/Description: 31299999/Miscellaneous Machinery ;Other Not Classified
5. Throughput/units in 2018:
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information
i
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-13 CD—BP-BV2 one bin vent filter 227 square feet of filter area
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft 0 (Feet/sec) Rate(Acfm)
ectangle(L x W)
(in 0.1 feet)
CEMT VERTICAL STACK 40.02 1.15 72.05 60 3739.28 Cement Silo Bin
Vent
35

- Operating Scenario:OS—27 Emission Source/Group ID: ES—BP—CS
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2018)
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%
018 1 018 �018 018
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission
Pollutants Pollutants Method Code (Net after Factor Ef Control
Tons/Year See Instructions all controls
2018
Criteria Emissions- Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission
Pollutants Code Pollutants Method Code (Net after Factor Ef Control
(Tons/Year) (See Instructions) all controls)
2018
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP CAS Emissions Emission Control
Pollutants (In HAP/TAPS Estimation, Emission
Efficiency EF Control
(see instructions) Method Code Factor
Alphabetical.Order) (Pounds/Year) (Net after all controls)
See Instructions
2018
36

PF-
COPY of RECORD Date Submitted: 6/14/2019 17:27:17
As entered in AERO
Facility Name: General Shale Brick,Inc.—Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit : 04384
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 2018
1. Emission Source ID(from permit)or ES—BP—FAS
Emission Source Group ID
2. Emission Source Description: Flyash silo(11 tons per hour capacity)
3. Operating Scenario ID/Description: OS—28/Flyash Silo
4. SCC Number/Description: 31299999/Miscellaneous Machinery ;Other Not Classified
5. Throughput/units in 2018:
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from-this Process Vented to Control 100
Device or Stack):
8. Control Device Information :
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-14 CD—BP—BH1 One ba filter 535 s aure feet of filter area
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
FLY VERTICAL STACK 44.95 1.15 72 60 3739.28 Flyash Silo Bin Vent
37

Operating Scenario: OS—28 Emission Source/Group ID:ES—BP—FAS
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2018)
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 8 25% �arch—May
18 25% une—Aug. 25% retNov. 25%
018
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission
Pollutants Pollutants . Method Code (Net after Factor Ef Control
Tons/Year) (See Instructions)' all controls
2018
Criteria Emissions— Emission Control
Criteria Estimation
(NAAQS) Pollutant Efficiency Emission
Pollutants Code Pollutants Method Code (Net after Factor Ef Control
(Tons/Year) (See Instructions) all controls)
2018
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
Pollutants (In Control
HAP/TAPS Estimation Emission
Alphabetical Order (see instructions) Method Code Efficiency Factor EF Control
P ) (Pounds/Year) (Net after all controls).
See Instructions
2018
38

- COPY of RECORD Date Submitted: 6/14/2019 17:27:17
As entered in AERO
Facility Name: General Shale Brick,Inc. -Moncure Facility Facility ID : 1900009
- 300 Brick Plant Road Permit: 04384
Moncure,NC 27559 County : Chatham
DAQ Region :RRO
North Carolina Department of Environment
_ p and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory-Calendar Year 2018
1. Emission Source ID(from permit)or ES-CD-8
Emission Source Group ID
2. Emission Source Description: Natural gas-fired rotary drum coatings dryer(250,000 Btu per hour heat input;
3.45 tons per hour drying capacity)
3. Operating Scenario ID/Description: OS-6/Rotary sand drum dryer(3.45 tons per hour)
4. SCC Number/Description: 36500301Brick Manufacture-Dryer;Raw Material Drying
5. Throughput/units in 2018: 0.110294 E6FT3/yr
(e.g.production or fuel use):
-- 6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
Btulunits
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
- asp 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-FG FUGITIVE(NO 1 72 Area= 1 ERP for Fugitive
STACK
sources
�' 39

Operating Scenario: OS—6 Emission Source/Group ID: ES—CD-8
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2018) .
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 250�oTulne—Z- g. 25% ept.—Nov. 25%
8 Varch—May
18 8 �018
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
I
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission
Pollutants Pollutants Method Code (Net after Factor Ef Control
" Tons/Year See Instructions all controls
2018
Criteria Emissions— Emission Control
NAA Pollutant Criteria Estimation Efficiency Emission
( QS) Code Ef Control
Pollutants Pollutants Method Code (Net after Factor
(Tons/Year) (See Instructions) all controls)
2018
CO CO 08
NOx NOx 0.01 08 100
I TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
Emissions Emission Control
TJ HAP/TAP CAS HAP/TAPS' Estimation Efficiency Emission
Pollutants (In Alphabetical Order EF Control
P ) (see instructions)
Method Code (Net after all Factor
(Pounds/Year)
See Instructions controls)
2018
Benzene - 71-43-2 0.00023 08 0.0021
Dichlorobenzene , 14— 106-46-7 0.00014 08 0.00123
Formaldehyde 50-00-0. 0.00827 08 0.075
Hexane n— 110-54-3 0.19853 08 1.8
Lead Unlisted Compounds
f (Specify and Component of PBC—Other 0.00006 08 0.0005
PBC
Naphthalene(Component of
POMTV) 91-20-3 0A0007 08 0.00061 -
Toluene 108-88-3 0.00037 08 0.0034
40

COPY of RECORD Date Submitted: 6/14/2019 17:27:17
-� As entered in HERO
Facility Name: General Shale Brick,Inc.—Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit: 04384
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 2018
1. Emission Source ID (from permit)or ES—Coal—CC
Emission Source Group ID
2. Emission Source Description: Coal crusher
3. Operating Scenario ID/Description: OS—33/Coal Processing System
4. SCC Number/Description: 39999997/Miscellaneous Industrial Processes;Other Not Classified
—� 5. Throughput/units in 2018:
a (e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur r
Ash Heat Content
Btu/units
- ' 7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
"j Device or Stack):
Y 8. Control Device Information
7 Order CS—ID . CD ID Control Device Description
f as listed inpermit)
1 CS-18 CD—Coal—CC One ba filter 4.7:1 air to cloth ratio
r �
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
D (in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
(in 0.1 feet)
P—Coal—CC VERTICAL STACK 30 2 75 18.56 3500 One Ba filter
-J
i
41

Operating Scenario: OS—33 Emission Source/Group ID: ES—Coal—CC
—` 10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2018)
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:
1 an—Feb +Dec o arch—May o une—Aug. o Sept.—Nov. o
018 25/0 018 25/0 018 25/° 018 25/o
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG� GHG Estimation Efficiency Emission CAS enc y Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2018
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAA Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2018.
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
Control
Pollutants (In HAP/TAPS Estimation Emission
Efficient EF Control
(see instructions) Method Code y Factor
Alphabetical Order) (Pounds/Year) See Instructions (Net after all controls)
2018
r
42

COPY of RECORD Date Submitted: 6/14/2019 17:27:17
-- As entered in AERO
Facility Name: General Shale Brick,Inc.—Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit: 04384
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 2018
1. Emission Source ID(from permit)or ES—K3K
Emission Source Group ID
2. Emission Source Description: POS—Natural gas/propane—fired brick tunnel kiln(25.9 million Btu per hour
heat input and 20.55 tons per hour maximum fired brick production rate) [2D
.1109 Case By Case MACT]AOS—Coal/Natural
3. Operating Scenario ID/Description: OS— 10/Natural gas/propane—fired kiln#3 (Uncontrolled)
4. . SCC Number/Description: 30500311/Brick Manufacture—Curing Firing; Curing and Firing:Gas—fired
Tunnel Kilns
5. Throughput/unitsin 2018:
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) ro
Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID. CD ID Control Device Description
as listed inpermit)
i
9.Emission Release Point ERP Information: (Sources .. nted 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/see) Rate(Acfm)
Rectangle(L x W)
i (in 0.1 feet)
-� ERP for ES—K3K,
EP-K3 VERTICAL STACK 35 4.92 99.95 33.79 38544.24 ES—K3D1 AND
ES—K3D2
43

Operating Scenario: OS— 10 Emission Source/Group ID: ES—K3K
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2018)
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 arch—May 25"�o line—Aug. 250�o �018
ept.—Nov. 25%
018 018 �018
13. Actual Emissions per Pollutant Listed
i
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG GHG Estimation Efficiency Emission
Pollutants CAS Ef Control
Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2018
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)
2018
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
_ S02 S02 08
VOC VOC 08
HAP/TAP Emissions Emission Control
CAS Estimation Emission
Pollutants (In (see instructions) HAP/TAPS Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) See Instructions (Net after all-controls)
2018
i
44

00
i
COPY of RECORD Date Submitted: 6/14/2019 17:27:17
- As entered in HERO
Facility Name: General Shale Brick,Inc.—Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit: 04384
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 2018
1. Emission Source ID (from permit)or ES—K3K
Emission Source Group ID
2. Emission Source Description: POS—Natural gas/propane—fired brick tunnel kiln(25.9 million Btu per hour
heat input and 20.55 tons per hour maximum fired brick production rate)(21)
.1109 Case By Case MALT]AOS—Coal/Natural
3. Operating Scenario ID/Description: OS—25/10/Natural gas/propane/coal—fired kiln#3
f
4. SCC Number/Description: 30500311Brick Manufacture—Curing Firing;Curing and Firing:Gas—fired
Tunnel Kilns
5. Throughput/units in 2018:
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
I
8. Control Device Information
Order CS—ID . CD ID Control Device Description
f as listed inpermit)
1 CS-15 CD—K3DLA Dry limestone adsorber
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
i
Rectangle(L x W)
(in 0.1 feet)
P—K3DLA VERTICAL STACK 75.1 4.92 470.03 43.6 49734.5 dry limestone
absorber
45

Operating Scenario:OS—25 Emission Source/Group ID: ES—K3K
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2018)
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 arch—May 25"�o rune—Aug. 25"�u �018
ept.—Nov. 25%
018 018
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
2018
Criteria Emissions— Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission
Pollutants
Code Pollutants Method Code (Net after Factor Ef Control
(Tons/Year) (See Instructions) all controls)
I
2018
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 CAS Emissions Control
Pollutants (In HAP/TAPS Estimation Efficiency Factor Emission
(see instructions) Method Code EF Control
Alphabetical Order) - (Pounds/Year) (Net after all controls)
See Instructions
2018
f
I 46

COPY of RECORD Date Submitted: 6/14/2019 17:27:17
As entered in AERO
Facility Name: General Shale Brick,Inc. —Moncure Facility Facility ID : 1900009
-- 300 Brick Plant Road Permit: 04384
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 2018
1. Emission Source ID(from permit)or ES—K4K
Emission Source Group ID
2. Emission Source Description: POS—Natural gas/propane—fired brick tunnel kiln(25.9 million Btu per hour
heat input and 20.55 tons per hour maximum fired brick production rate) [2D
.1109 Case By Case MACT]AOS—Coal/natural
3. Operating Scenario ID/Description: OS—21/Coal/Natural gas/Propane—fired kiln#4
4. SCC Number/Description: 3050031 IBrick Manufacture—Curing Firing;Curing and Firing: Gas—fired
Tunnel Kilns
5. Throughput/units in 2018: 148609 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 100
Device or Stack):
f
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-11 CD—K4DLA Dry limestone adsorber
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/see) Rate(Acfm)
Rectangle(L x W)
_ (in 0.1 feet)
P—K4DLA VERTICAL STACK 75.13 4.92 469.' 43.64 49780.13 Dry limestone
adsorber on Kiln 4.
,.- 47

_ Operating Scenario: OS—21 Emission Source/Group ID: ES—K4K
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year-2018)
Hours per Day ( 8 ) . Days per Week ( 5 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec o arch—May o tine—Aug. o Sept.—Nov. o
018 25/0 018 25/0 018 25/0 1 25/o
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
2018
-- Emission
Criteria Emissions— Estimation Control
Pollutant Criteria Method Efficiency Emission
(NAAnt Code Pollutants Code (Net after Factor Ef Control
Pollut ants
_ «
(Tons/Year) (See all controls)
Instructions
2018
CO CO 61.67 08 0
NOx NOx 26.01 08 0
TSP TSP 51.56 08 0
PM10 PM10 51.56 08 0
i
PM2.5 PM2.5 51.56 08 0
S02 S02 0.85 08 0
VOC VOC 1.78 08 0
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
2018
Arsenic Unlisted Compounds( ASC—Other 4.60688 08 0 0.000031 AFTER
Specify Component of ASC
Benzene 71-43-2 430.9661 08 0 0.0029 AFTER
Cadmium Metal(elemental 7440-43-9 2.22914 08 0 0.000015 AFTER
unreacted,Component of CDC
Chlorine 7782-5.0-5 193.1917 08 0 0.0013 AFTER
Chromic acid(VI)(Component of SolCR6 CRC 7738-94-5 7.57906 08 0 0.000051 AFTER
Di 2—eth lhex 1 hthalate DEHP 117-81-7 297.218 08 0 0.002 AFTER
Dichlorobenzene ,1,4— 106-46-7 7.13323 08 0 0.000048 AFTER
48

-- Ethyl chloride chloroethane 75-00-3 84.70713 08 0 0.00057 AFTER
Fluorides(sum of all fluoride compounds) 16984-48-8 1371.66107 08 0 0.00923 AFTER
'
Formaldehyde 50-00-0 22.3 08 0
_- Hydrogen chloride(hydrochloric 7647-01-0 3905.44452 08 0 0.02628 AFTER
acid
Hydrogen fluoride(hydrofluoric
acid as mass of HF—Component of 7664-39-3 857.47393 08 90 0.00577 AFTER
Fluorides
Lead Unlisted Compounds(Specify PBC—Other 22.29135 08 0 0.00015 AFTER
and Component of PBC
Mercury,vapor(Component of HGC 7439-97-6 1.11457 08 0 0.0000075 AFTER
Methyl chloride 74-87-3 99.56803 08 0 0.00067 AFTER
Methyl iodide 74-88-4 13.82064 08 0 0.000093 AFTER
Naphthalene(Component of POMTV) 91-20-3 9.65959 08 0 0.000065
Nickel metal(Component of NIC 7440-02-0 10.69985 08 0 0.000072 AFTER
Selenium Compounds SEC 34.18007 08 0 0.00023 AFTER
Styrene 100-42-5 2.97218 08 0 0.00002 AFTER
Toluene 108-88-3 23.77744 08. 0 0.00016 AFTER
49

f
p to i�o-z DP+�-r
COPY of RECORD Date Submitted: 6/14/2019 17:27:17
As entered in AERO
Facility Name: General Shale Brick,Inc.—Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit : -04384
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 2018
1. Emission Source ID(from permit)or ES—RUMBLE
Emission Source Group ID
2. Emission Source Description: Rumbler system
3. Operating Scenario ID/Description: OS—36/Rumbler tumbles blocks in a rotating drum in order to create an
4. SCC Number/Description: 30500397Brick Manufacture; *Other Not Classified
5. Throughput/units in 2018:
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
i
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 ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x
)
Kin 0.1 feet)
P-RUMBLE VERTICAL STACK 44.95 1 1.312 1 72.05 40.02 3246.27 1 Rumbler Ba house
50

Operating Scenario: OS—36 Emission Source/Group ID:
ES—RUMBLE
_ 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2018)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year .( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec o rch—May o ne—Aug. o Sept.—Nov. o
018 25/0 �078 25/0 �OU18 25�O 2018 25/o
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2018
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)
2018
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 CAS Emissions Estimation Control Emission
Pollutants (in (see instructions) Method Code HAP/TAPS Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2018
_i
_r
51

Facility Total CY 2018 Emissions Summary
COPY of RECORD Date Submitted: 6/14/2019 17:27:17
As entered in AERO
Facility Name: General Shale Brick,Inc. -Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit: 04384
Moncure,NC 27559 County: Chatham
DAQ Region :RRO
North Carolina Department of Environment and Natural Resources
i Division of Air Quality
Air Pollutant Point Source Emissions Inventory-Calendar Year 2018
Record Facility-Wide Totals From all Permitted and Non-Permitted Air Pollutant Emission Sources
Green House Gases Pollutants(GHG)
i
Actual Emissions Tons/Year
Pollutant CAS 2018 2017 % Change
Criteria Pollutants
Actual Emissions Tons/Year
Pollutant
CAS 2018 2017 % Change
CO CO 84.7 82.42 2.7663174%
_ NOx NOx 33.3 32.39 2.8095088%
PM TSP TSP 69.47 66.78 4.028156%
PM 10 PM 10 66.26 64.42 2.856262%
PM2.5 PM2.5 66.26 64.38 2.9201694%
S02 S02 0.85 .83 2.4096434%
VOC VOC 4.68 4.57 2,4069946%
Hazardous Air Pollutants(HAP and/or Toxic Air Pollutants TAPs
Actual Emissions Pounds/Year
Pollutant CAS 2018 2017 % Change
Pollutant Group:Arsenic Compounds(total mass of elemental AS,arsine and all inorganic compounds) Group
Sum:4.60688
Arsenic_ Unlisted Compounds (Specify
Component of ASC ASC-Other 4.60688 4.49469 2.496062%
ollutant Grou :Cadmium compound total mass inc elemental metal Group Sum:2.22914-
Cadmium Metal(elemental unreacted,
Component of CDC 0-43-
7449 2.22914 2.17485 2.4962666%
Pollutant Grou :Chromium VI Soluble Chromate Com ounds(Component of CRC Group
rou Sum:7.57906
Chromic acid(VI)(Component of
So1CR6 CRC) 7738-94-5 7.57906 7.39449 2.496052%
Pollutant Grou :Chromium-All/Total Inc Chromium VI cate ories,metal and Others Grou Sum:7.57906
Chromic acid(VI)(Component of
7738-94-5 7.5906 7449SoICR6 CRC 2.496052%
Pollutant Grou :Lead and Lead co ounds GroupSum:22.29141
_F Lead Unlisted Compounds(Specify PBC-Other 22.29141 21.74856 2.4960296%
52

and Component of PBC
Pollutant Group:Mercury Compounds-all total mass,inc H&Vapor Group Sum:1.11457
Mercury,vapor(Component of HGC 7439-97-6 1.11457 1.08743 2.4957948%
Pollutant Grou :Nickel Compounds, sum total mass,inc elemental Group Sum:10.69985
- Nickel metal(Component of NIC 7440-02-0 10.69985 10.43928 2.4960585%
Pollutant Grou :Pol c clic Organic Matter(Specific Com ounds from OA PS for TV Group Sum:9.65966
Naphthalene(Component of POMTV 91-20-3 9.65966 9.42442 2.4960685%
Benzene 71-43-2 430.96634 420.47123 2.496037%
Chlorine 7782-50-5 193.1917 188.487 2-4960325%
Di(2-eth lhex 1 hthalate DEHP 117-81-7 297.218 289.98 2.4960258%
Dichlorobenzene , 1,4- 106-46-7 7.13337 6.95966 - 2.4959533%
Ethyl chloride chloroethane 75-00-3 84.70713 82.6443 2.4960318%
Fluorides(sum of all fluoride 16984-48-8 1371.661 2319.84 -40.872604%
compounds)
Formaldehyde 50-00-0 22.30827 23.90827 -6.6922464%
Hexane,n- 110-54-3 0.19853 .19853 0.0%
H dro en chloride(hydrochloric acid 7647-01-0 3905.4446 4349.7 10.213477%
Hydrogen fluoride(hydrofluoric acid
as mass of HF-Component of 7664-39-3 857.47394 1449.9 -40.85979%
Fluorides
Methyl chloride 74-87-3 99.56803 97.1433 2.4960325%
Methyl iodide 74-88-4 13.82064 13.48407 2.496055%
Selenium Compounds SEC 34.18007 33.34.77 2.4960365%
Styrene 100-42-5 2.97218 2.8998 2.4960282%
Toluene 1 108-88-3 23.77781 1 23.19877 2.4959884%
53

- COPY of RECORD Date Submitted: 6/14/2019 17:27:17
As entered in AFRO
Facility Name: General Shale Brick,Inc.—Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit• 04384
Moncure,NC 27559 County : Chatham
DAQ Region :RRO
Comments From Facility:
54

_ SECTION 2
2018 SUPPORTING EMISSION CALCULATIONS
General Shale Brick, Inc.-Moncure, NC Facility 1.CY 2018 Emissions Inventory
Trinity Consultants

Title: 2018 Air Emission Inventory
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
Critical Parameters Table
Parameter Value
Combustion SOUrces-Ca e Fear
Actual Brick Production om cr ccur
Actual Sawdust Usage 0 tPY
Combustion Sources-Brickhaven-Kiln 3 and Associated Dryers
Actual Brick Production(Natural Gas) 0 tPY
Actual Brick Production(Coal&N(;) 0 tPY
Actual Gas Usage 0 scf/ r
Actual Coal Usage 0 tPY
Combustion Sources-Brickhaven-kiln 4 and Associated Dryers
Actual Brick Production(Natural Gas) 148,N i1J tpy
Actual Brick Production Coal&NG 0 tPy
Actual Brick Production(Coal&NO) 0 lb/hr
Actual Gas Usage 282,869,760 scf r
Actual Coal Usage 0 t V
Wood Waste System-Cale Fear
Number of Cyclones I
Sawdust preparation fir cr
Clay Handling Operations
Actual Raw Material Processed 233,360 tpy
Hours of operations 2.024 hr/ r
Intersite Conveyor
Proic„ I hroueh gut t
Sand Drver-Ca e Fear
I lours of o erations I ?rl hi-A r
Texturing O erations
Actual Brick Production 143.609 tpy
Ba house Efficiency 99.8%
Hours of operation-Brick Haven 3,500 hr/ r
1 lours of operations-Cape Fear 0 hr/ r
Vacuum Systems
flours of operations-Cape Fear VS 1 0 hr/ r
Hours of operations-Brick Haven VS2 1.500 hr/ r
Hours of operations-Brick Haven VS3 -Kiln 3 1000 hr/ r
a
Flvash silo
Fk ash siloThroueh tit tic
Cement Silo
Cement silo I hi- Ugh nut [»
Mixer Loading
Miser Luaduu Throur01 iut I t
Aggrcgate Loading
Atgrc,atcLoading Ihauial>>ut �
Rumbler
I lours of o.emtions fir cr
Fuel Usage
Diesel Tank 58,7 18 gal/yr
Gasoline Tank 3,799 I/ r
Waste Oil Tank 0 al/ r
Motor Oil Tank 110 al/ r
Brick Oil Tank 6,038 al/ r
Gear Oil Tank 600 al/ r
Reference:
Information Provided by Warren Paschal,General Shale Brick,Inc.,June 11,2019
Support Calculations File: General Shale Moncure CY2018 El 2019-06-11
Printed:6/12/2019 Page 1 of 34 Sheet: Input

1
i
f
Title: 2018 Air Emission Inventory
Source ID 0: FSKI,ES-K2,ES-SDI
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility iD H 1900009
Brick Processing System-Cape Fear
— AERO: G-66 _
Description: After the wet clay is formed and coated it passes through the brick dryer and the kiln. The kiln is
sawdust fired. Combustion products and heat generated by the kiln are vented to the drum dryer
which dries the sawdust. From the drum dryer the exhaust is vented to the atmosphere. However,not
all of the heat from the kiln is vented to the wood dryer. Instead,some evaporative heat is routed to
the brick dryers and vented to atmosphere.
Approach: The AP42 Section 11.3 is used to estimate the emissions from these emission units,except for
fluoride and hydrogen fluoride factors developed from a GSB test at Moncure.
,�'; gr:t'araaieter�?', ;- z`,:.:.��;`•xd .�. Value';};
Actual Brick Production 0
Actual Sawdust Usage tpy
' EMISSION CALCULATIONS
Emissions are calculated by the following equation: -
i
Yeady Emissions-
- 3
Emission Factor(lb/tons brick)•Brick Production(tpy)=Emissions(lb/yr)
Emissions(lb/yr)/2000lb/ton=Emissions(tpy)
..._�I Note:The Formaldehyde emissions are multiplied by the wood usage instead of bricks usage.
~4
i
i
E
Support calculations File:General Shale Moncure CY2018 El 20194)611
Printer:61122019 Page 2 0134
. Sheet:Brick-CF(G-66)

Source: ES-KI,ES-K2,ES-SDI Sawdust[Gins 1&2 and sawdust dryer
Actual Annual Process Throughput: Tons/yr
Brick Win Fuel: Wood
Annual-.,'<,.-R Annual
,
issi o iia'fe
i�"-
A
mIsSIT';FactoC.(l
CAS N0w.. E' MISSIg MNO
produced) bs/y r
fired
(TP
PM 0.675 d 0 0.00
PM-10 0.675 ' 0 0.00
PM 2.5 0.675 d 0 0.00
SO2 0 0.00
NOx d 0 0.00
VOC 0.18 0 0.00
CO 0.344 d 0 0.00
1,4-dichlorobenzene 36 106- 0.00E+00 0.00E+00
2-butanone(MEK) 70 78-93-3 2.20E-04 ab 0.00E+00 0.00E+00
2-methylphenol(cresol) 35 9548-7 2.40E-09 nb 0.00E+00 0.00E+00
Acrylonitrile 4 107-13-1 1.90E-05 0.00E+00 0.00E+00
Antimony HAP ANTIMONYCPDS 2.80E-06 0.0013+00 0.00E+00
Arsenic 9 ARSENICCPDS 2.10E-05 U013+00 0.00E+00
Benzene 12 71-43-2 5.6013-04 0.00E+00 0.00E+00
Beryllium 16 BERYLCPDS 1.1013-07 0.00E+00 0.0013+00
Bis(2-ethylhexyl)phthalate;di(2-
ethylhexyl)phthalate 39 117-87-7 1.40E-04 n6 0.00E+00 0.00E+00
Bromometbane(Methyl Bromide) HAP 74-83-9 4.40E-05 nb 0.00E+00 0.00E+00
Cadmium ' 23 CADMIUMCPDS 2.20E-05 0.00E+00 0.00E+00
Carbon Disulfide 27 75-15-0 1.80E-05 a6 0.00E4-00 0.00E+00
Carbon tetrachloride 28 56-23-5 3.80E-07 0.00E+00 0.00E+00
Chlorine 29 0.0013+00 0.00E+00
Chloroethane(Ethyl Choroethane) HAP 75-00-3 0.00E+00 0.00E+00
Chloroform 31 67-66-3 3.8013-07 0.00E+00 0.00E+00.
Chloromethane(Methlyl Chloride) HAP 74-87-3 0.0014 ab 0.00E+00 0.00E+00
Chromium(expressed as chromic
acid) HAP CROMCPDS 4.8013-05 0.00E+00 0.00E+00
Cobalt HAP 7440-48-4 0.0013+00 0.00E+00
Diethylphthalate HAP 84-66-2 - 0.00E+00 0.00E+00
Dimethylphthalate HAP 131-11-3 2.40E-09 0.00E+00 0.00E+00
Di-n-butylphthalate HAP 84-74-2 1.60E-05 0.0013+00 0.00E+00
Ethylbenzene HAP 10041-4 I.00E-05 'b 0.00E+00 0.00E+00
Fluorine 50 0.0013+00 0.0013+00
Formaldehyde 51 50-00-0 6.63E-03 0.00 0.00E+00
Hydrazine HAP 0.00E+00 0.00E+00
Hydrogen Fluoride 59 7664-39-3 0.23 b 0.00E+00
HCl 57 7647-01-0 0.11 0.00E+00
Hydrogen Sulfide 60 7783-064 0-00E+00 0.00E+00
lodomethane(Methyl Iodide) HAP 74-88-4 2.40E-04 0.00E+00 0.00E+00
Lead HAP LEADCPDS 1.20E-04 0.60E+00 0.00E+00
M-/p-Xylene HAP 108-38-3/106-42-3 2.90E-65 0.0013+00 0.00E+00
Manganese 62 MANGCPDS 4.80E-04 0.0013+00 0.00E+00
I I I-Trichloroethane
(methylchloroform) 68 71-55-6 5.20E-.07 0.00E+00 0.00E+00
Methylene Chloride 69 74-87-3 6.20E-05 0.00E+00 0.00E+00
Mercury 66 MERCCPDS 1.1 OE-05 0.00E+00 0.00E+00
Naphthalene HAP 91-20-3 . 2.40&09 0.00E+00 0.00E+00
Nickel 75 NICKCPDS 3.40E-05 0.00E+00 0.00E+00
o-Xylene HAP 95-47-6 7.30E-06 0.00E+00 0.00E+00
Ozone 0.00E+00 0.00E+00
Perchloroe.thylene
(Tetrachloroethene) 81 127-184 3.80E-07 A 0.00E+00 0.00E+00
Phenol 82 108-95-2 1.00E-04 0.00E+00, 0.00E+00
Phosphine 71 0.00E+00 I 0.00F+00
,Phosphorus HAP 7723-14-0 1 5.50E-04 I- I 0.00E+001 0.00E+00
Support Calculations Re:General Shale Monwre CY2018 El 2019-0&11
P,irrtert 611202019 Page 3 of 34 Sheet Brick-CF(G,66)

i
Selenium HAP SEC 4.70E-05 " 0.00E+00 0.00E+00
Styrene 91 100.42-5 4.20E-06 ab 0.00E+00 0.00E+00
Toluene 97 108-88-3 4.30E-04 ab 0.00E+00 0.00E+00
Total Fluorides(including HF) 50 16984-48-8 0.27 b 0.00 0.00E+00
Trichlorofiuoromethane 100 75-69-4 I.00E-06 a6 0.00E+00 0.00E+00
Vinyl acetate HAP 1 108-054 1 1.90E-07 ab 0.00E+00 0.00E+00
Xylene 104 1 1330-20-7 1 3.63E-05 0.00E+00 O.00E+00
Emission factors from AP42,Section 11.3,8/97
Table 11.3-7 for sawdust fired kilns and sawdust dryer.
ab Table 11.3-6 for sawdust fired kilns and sawdust dryer. -
Table 11.3-2 for sawdust fired kiln and sawdust dryer.
'd Table 11.3-3 for sawdust fired kilns.
Table 11.3-5 for sawdust fired kilns and sawdust dryer.
'r Table 11.34 for uncontrolled sawdust or natural gas fired tunnel kiln.
b Based on General Shale Brick Moncure Facility Stack Testing-DAQ requires TF=Fluorides of 0.04 lb/ton+HF of 0.23 lb/ton)
Emission factor provided by NCDENR,the emission factor basis is pound of emissions/tons of wood;
therefore,the factor is multiplied by the wood used.
Sawdust Usage from input Table= Ipy
d Testing was performed on Kiln 1 and Kiln 2 in June 2006.Emission Factors are as follows:
Process weight rate during test for both kilns 22.3 ton/hr
" � As � � Highest Emissions Rate EmJsston .:;
Pollutants L,s r Tested(Iblhr} Factor(Ibltou)
PM 15.05 0.675
CO 7.68 0.344
S02 data was from a September 27,2004 engineering test on Kiln 3 with
a process weight rate of. 19.58 tons/hr
Highest$tun Emissions EmISSIOn
Pollutarifr Rate,csted(Ib/tir),;,'Facfor(Ib/ton
S02 0.56 0.029~
S02 factor for wood combustion AP-42Section 1.6 0.025 lb/MMBtu
MMBtu for wood=Tons wood fired•2000 Ib/ton•8000 Btu/Ib
MMBtu for wood= 0 MMBtu
S02 Emissions=Tested lb/ton•Actual Production ton/yr+Wood Combustion Factor Ib/Mmbtu•MMBtuyr fired
S02 Emissions= - Ibs/yr
Support Calcula8ans - Fde:General Shale Moncure CY2018 EJ 201MS-11
Printed:6l1212019 Page 4 of 34 Sheet:BridcLF(G-66)

Title: 2018 Air Emission Inventory
Source ID 9: ES-K3K
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID N: 1900009
Brick Processing System-Brick Haven-Kiln 3 .
Source: ES-K3K Kiln 3
AERO: GR12
Actual Brick Production: 0 Tons/yr
Coal Fired 0 Tons/yr
Brick Kiln Fuel: CoaUNG
60%Coal
40%Natural Gas
Control Eff,of HF 90% (NESHAP Requirement)
Uncontrolled
Uncontrolled, Emtsston �� 1
x Emtsston ;
;TAP NO Refs Factor for Tested< t Total
- � Factor for Coal : f
¢ 3 > � �: s -� 'Natural.Gas Emtsston i ;'Annual) Annual
from AP 42
Pollutant K; 2 from AP-42 Ref Factors r Ref Emtsstons ,- Em�ss�ons
,��a �� »t, ., ��.^r: , ,.:,.lb/ton `,. .�,__. :•(Ib/ton) Ib/[on), (Ib/ r), N(ton%,Xr)';(
PM 4.12E-01 9 0.00 0.00E+00
PM-10 2.03E-01 9 0.00 0.00E+00
PM-2.5 2.03E-01 9 0.00 0.00E+00
S02 38.000 f 2.86E-02 d 0.00 0.00E+00
NOx 8.13E-01 a 0.00 0.00E+00
VOC 2.40E-02 ad 2.40E-02 ad 0.00 0.00E+00
CO 8.00E-01 ab 0.83 ai . 0.00 0.00E+00
Chlorine 29 1.30E-03 of 0.00 0.00E+00
HF 59 3.81E-01 d 0.00 0.00E+00
HCI 57 5.82E-02 d 0.000 0.00E+00
I I I-Trichloroethane 68 1.70E-05 ae 4.70E-06 of 0.00E+00 0.00E+00
(methylchloroform)
Methylene Chloride 69 8.00E-07 ac 0.00E+00 0.00E+00
Perchloroethylene 81 2-80E-06 of 0.00E+00 0.00E+00
(Tetrachloroethene)
l,l-dichloroethane HAP 5.00E-06 a` 0.00E+00 0.00E+00
.1,4-dichlorobenzene 36 3.20E-06 ae 4.80E-05 of 0.00E+00 0.00E+00
2-butanone.(MEK) 70 2.50E-04 ac 2.20E-04 of 0.00E+00 0.00E+00
2-Hexanone NA 9.40E-07 ae 8.50E-05 of 0.00E+00 0.00E+00
2-methylphenol(cresol) 35 2.20E-06 ac 0.00E+00 0.00E+00
2-methylnaphthalene NA 1.70E-06 ac 5.70E-05 of 0.00E+00 0.00E+00
Antimony NA 2.70E-05 a1i 0.00E+00 0.00E+00
Acetone NA 6.80E-04 a` 1.70E-03 of 0.00E+00 0-00E+00
Arsenic 9 1.30E-04 ag 3.10E-05 ah 0.00E+00 0.00E+00
Benzene 12 2.90E-04 d0 2.90E-03 a0 0.00E+00 _ 0.00E+00
Benzoic Acid 2.50E-04 ae 0.00E+00 0.00E+00.
Beryllium. 16 1.60E-05 ag 4.20E-07 all 0.00E+00 0.00E+00
Bis(2-ethylhexyl)phthalate;di(2- 39 7.30E-05 ac 2.00E-03 of 0.00E+00 0.00E+00
ethylhexyl)phthalate
Bromomethane(Methyl Bromide) HAP 2.40E-05 ae 0.00E+00. 0.00E+00
Butylbenzylphthalate NA 1.20E-06 ac 1.80E-05 of 0.00E+00 O.00E+00
Cadmium 23 1-50E-05 ah 0.00E+00 0.00E+00
Carbon Disulfide 27 2.30E-06 ae 430E-05 of 0.00E+00 0.00E+00
Support Calculations- File:General Shale Moncure CY2018 El 2019-06-11
Printed:6112/2019 - Page 5 of 34 Sheet:Brick-BH(ES-K3K Gl2)NG&.Coal

Carbon tetrachloride 28 1.00E-07 '° 0.00E+00 0.00E+00
Chlorobenzene HAP 2.10E-05 " 0.00E+00 0.00E+00
Chloroethane(Ethyl HAP 1.10E-05 aO 5.70E-04 cur 0.00E+00 0.00E+00
Chloroform 31 1.00E-07 " 0.00E+00 0.00E+00
Chloromethane(Methyl Chloride HAP 1.10E-04 6.70E-04 at 0.00E+00 0.00E+00
Soluble Chromate Compounds 5.10E-05 ah 0.00E+00 0.00E+00
Cobalt 2.10E-06 'h 0.00E+00 0.00E+00
Dibenzofuran NA 3.60E-07 a` 0.00E+00 0.00E+00
Diethylphthalate HAP 1.40E-06 'e 2.40E-04 cur 0.00E+00 0.00E+00
Dimethylphthalate HAP 7.80E-07 '° 0.00E+00 0.00E+00
Di-n-butylphthalate HAP 1.40E-04 cur 0.00E+00 0.00E+00
Di-n-octylphthalate 1.20E-05 '= 0.00E+00 0.00E+00
Ethylbenzene HAP 2.10E-05 a° 4.40E-05 of 0.00E+00 0.00E+00
Formaldehyde 51 7.50E-02 b 0.00E+00 0.00E+00
lodomethane(Methyl Iodide) HAP 9.30E-05 of 0.00E+00 0.00E+00
Isophorone HAP 3.00E-05 cue 0.00E+00 0.00E+00
Lead NA 1.50E-04 ah 0.00E+00 0.00E+00
j M-/p-Xylene HAP 1.30E-04 cue 6.70E-05 of 0.00E+00 0.00E+00
Manganese 62 2.90E-04 ag 2.90E-04 'h 0.00E+00 0.00E+00
Mercury 66 9.60E-05 ag 7.50E-06 ah 0.00E+00 0.00E+00
Naphthalene HAP 6.90E-06 a' 6.50E-05 cue 0.00E+00 0.00E+00
i
Nickel 75 7.20E-05 A 0.00E+00 0.00E+00
o-Xylene HAP 4.70E-05 ac 5.80E-05 aQ 0.00E+00 0.00E+00
Perchloroethylene at 0.00E+00 0.00E+00
(Tetrachloroethene) 81 2.80E-06
Phenol 82 3.50E-05 cue 8.60E-05 a< 0.00E+00 0.00E+00
Phosphorus HAP 9.80E-04 ag 0.00E+00 0.00E+00
Selenium NA 2.30E-04 ah 0.00E+00 0.00E+00
Styrene 91 1.00E-07 ac 2.00E-05 aQ 0.00E+00 0.00E+00
Toluene 97 2.50E-04 - 1.60E-04 aB 0.00E+00 0.00E+00
Total Fluorides 50 6.10E-01 0.00E+00 0.00E+00
Trichlorofluoromethane 100 1.40E-05 ac 0.00E+00 0.00E+00
Vinyl acetate HAP 1.00E-07 ac 0.00E+00 0.00E+00
'Emission factors from AP42,Section 11.3,8/97
Table 11.3-1 for uncontrolled coal-fired and natural gas-fired kilns.
PM for condensible PM= 0.59 lb/ton
'bTable 11.3-3 for coal-fired and natural gas-fired kilns.
"Table 11.34 for coal-fired and natural gas-fired kilns
a4Table 11.3-5 for brick kilns.
"Table 11.3-6 for coal-fired kilns.
"Table 11.3-6 for natural gas-fired kilns
"Table 11.3-7 for coal-fired kilns.
't'Table 11.3-7 for natural gas-fired kilns.
"Factor is from AP42 Background Document testing at
Marseilles Brick which has the same type of kiln
Soluble Chromate Compounds is the regulated NC TAP
bEmission'factors from AP-42,Section 1.4,7/98. The emissions factor in in lblmmft;of gas. The actual gas rate:
Formaldehyde Emission Factor=
0.0 MMBnt/hr/1020 Btu/fe.10'BttvWIN Btu/I0^(ft'ftAMft')= 0.0000 mmft3/hr
` Using AP42 background information,assume that total fluorides emission factor is 60%of the HF emission factor
Also DAQ requires that total fluorides include HF,therefore TF=fluorides+HF(lb/yr)
TF=((0.381 lb/ton.0.60)+0.381 lb/ton)•Brick Production ton/yr•(1 -CE)
°Testing was performed on Kiln 4 on February 10,2006. Emissions Factors are as follows:
Process weight rate during test 19.93 ton/hr
Support Calculations File:General Shale Moncure CY2018 El 2019-06-11
Printed:W122019 - Page 6 or 34 Sheet:Brick-BH(ES-K3K G12)NG 8 Coal

EmissionsrRate Emrsslon Factor
Pollutant ... :, mTes4e�,(Ib/hr)� �� "
z (1p/ton),
HFs 7-6 0.381
HCI• 1.16 0.058
PM 2.25 0.113
PM filterable 2.25 0.113
S02.. 0.56 0.029
"Total Fluorides are 60%of HF
`•SO2 data was from a September 27,2004 engineering test on Kiln 3 with
iia process weight rate of: 19.58 tons/hr
`Test Results of Tested Highest run from Kiln and Dryer from Nov.11,2004 Indiana stack test=
j NOx Emission Factor= 9.67 Ib/hr/ 11.89 ton/hr
I
NOx Emission Factor= 0.813lb/ton
rAP42 coal combustion
Ap-42 Emission Factor:Section 1.1 Table 1.1-3 38S lb/ton coal fired
Sulfur Content of Fuel 1.000%
S02 EF= 38 lb/ton coal fired
r
e A coal fired kiln with a DLA was tested at a GSB site in VA.A total of three(3)test runs for Particulate Matter was conducted on February 23,2005
and a total of three(3)test runs for Particulate<10 microns was conducted on February 24,2005.
Highest Run Production Data 29,624 Ibs of brick/hr
Emission Factors are as follows:
Average;;"
Emissions Rate `Emission Factor
Pollutant - Tested
- PM 6.1 0.412
PMlo 3 0.203
PM,, 3 0.203
Support Calculations File:General Shale Moncure CY2018 El 2019-06-11
Printed:6/122019 Page 7 of34 Sheet Brick-BH(ES-K3K GI2)NG&Coal

Title: 2018 Air Emission Inventory
Source ID#: ES-K3D1,ES-K3D2,ES-K3D3
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
I4
Source: ES-K3D1,ES-K3D2,ES-K3D3
Brick Dryers 1,2,and 3 on Kiln 3
AERO: GR12
Actual Production: - Tons/yr
Brick Dryer Fuel: NG/Propane
- E►n1SSlOn Factors Emission Ratea Em>tss�o4
s
Pollutant z (lb�ton fired backs produced) (Ib/yr) Rate(TPI
-.
PM 0.187 ac 0.00 0.00
PM-10 0.187 ac 0.00 0.00
PM-2:5 0.187 ac 0.00 0.00
i S02 0.00
NOx 0.098 as 0.00 0.00
VOC 0.03 ab 0.00 0.00
CO 0.31 as 0.00 0.00
Formaldehyde 1.55E-01 b
a Emission factors from AP-42, Section 11.3,8/97
as Table 11.3-3 for brick dryer with supplemental gas burner
ab Table 11.3-5 for brick dryer.
ac Table 11.3-1 for brick dryer.
b The formaldehyde emissions from the dryer are included in the kiln calculation.
I` Printed:6/12/2019 Support Calculations File: General Shale Moncure CY2018 El 2019-0&11
Page 8 of 34 Sheet Brick-BH(ES-M—G12)(total)

Title: 2018 Air Emission Inventory
Source ID#: ES-K4K
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
Brick Processing System-Brick Haven-Kiln 4
Source: ES-K4K Kiln 4
AERO: ES-K4K
Actual Brick Production: 148,609 Tons/yr
Coal Fired 0 Tons/yr
Brick Kiln Fuel: Coat(NG
Percentages if Coal Fired: 60%Coal
40%Natural Gas
Control Eff.of HF 90% (NESIJAP Requirement)
1N CY 2018 Fired NG Onh
Uncontrolled
Emission
TAP NO. Factor for Tested
Natural Gas Emission Annual Total Annual
Pollutant from AP-42 Ref Factors Ref Emissions Emissions
(lb/ton) (lb/ton) (lb/yr) ((on/yr)
NNOx
1.04E-01 e,as 103,1 12 51.56
1.04E-01 e,as 103,112 51.56
1.04E-0I e,as 103,112 51.56
2.86E-02 d 1,700 0.85
3.50E-01 a6 52,013Z1.
2.40E-02 as 3,5670.83 123,34529 1.30E-03 t 193HF 595.77E-03 e857.4HCI 572.628E-02 e3,90b
I I 1-Trichloroethane 68 470E-06 at 6.98E-01 3.49E-04
(methyl chloroform)
Methylene Chloride 69 0.00E+00 0.00E+00
Perchloroethylene 81 2.80E-06 "f 4.16E-01 2.08E-04
(Tetrachloroethene)
1,1-dichloroethane HAP 0.00E+00 0.00E+00
1,4-dichlorobenzene 36 4.80E-05 of 7.13E+00 3.57E-03
2-butanone(MEK) 70 2.20E-04 'r 3.27E+01 1.63E-02
2-Hexanone NA 8.50E-05 of 1.26E+01 6.32E-03
2-methylphenol(cresol) 35 0.00E+00 0.00E+00
2-methyInaphthalene NA 5.70E-05 of 8.47E+00 4.24E-03
Antimony NA 2.70E-05 ah 4.01E+00 2.01E-03
Acetone NA 1.70E-03 of 2.53E+02 1.26E-01
Arsenic 9 3-10E-05 h 4.61E+00 2.30E-03
Support Calculations File:General Shale Moncure CY2018 E12019-06-11
Printed:6/12/2019 Page 9 of 34 Sheet:Brick-81-1(ES-K4K)NG 8 Coal

Benzene 12 2.90E-03 4.31E+02 2.15E-01
Benzoic Acid 0.00E+00 0.00E+00
Beryllium 16 4.20E-07 ah 6.24E-02 3.12E-05-
Bis(2-ethylhexyl)phthalate; 39 2.00E-03 of 2.97E+02 1.49E-01
di(2-ethylhexyl)phthalate
Bromomethane(Methyl HAP 0.00E+00 0.00E+00
Bromide)
Butylbenzylphthalate NA 1.80E-05 of 2.67E+00 134E-03
Cadmium 23 1.50E-05 ah 2.23E+00 1.11 E-03
- Carbon Disulfide 27 4.30E-05 of 6.39E+00 3.20E-03
Carbon tetrachloride 28 0.00E+00 0.00E+00
Chlorobenzene HAP 0.00E+00 0.00E+00
Chloroethane(Ethyl HAP 5.70E-04 of 8.47E+O1 4.24E-02
Chloride)
- Chloroform 31 0.00E+00 0.00E+00
Chloromethane(Methyl HAP 6.70E-04 of 9.96E+01 4.98E-02
Chloride)
Soluble Chromate 5.10E-05 ab 7.58E+00 3.79E-03
Compounds
Cobalt 2.10E-06 A 3.12E-01 1.56E-04
Dibenzofuran NA 0.00E+00 0.00E+00
Diethylphthalate HAP 2.40E-04 of 3.57E+01 1.78E-02
Dimethylphthalate HAP 0.00E+00 0.00E+00
Di-n-butylphthalate HAP 1.40E-04 of 2.08E+01 1.04E-02
Di-n-octylphthalate 0.00E+00 0.00E+00
Ethylbenzene HAP 4.40E-05 of 6.54E+00 3.27E-03
Formaldehyde 51 7.50E-02 b 2.12E+01 1.06E-02
lodomethane(Methyl HAP 9.30E-05 of 1.38E+01 6.91 E-03
Iodide)
Isophorone HAP 0.00E+00 0.00E+00
Lead NA 1.50E-04 al' 2.23E+01 1.1 t E-02
M-/p-Xylene HAP 6.70E-05 of 9.96E+00 4.98E-03
Manganese 62 2.90E-04 A 4.31E+01 2.15E-02
_ Mercury 66 7.50E-06 ah 1.11 E+00 5.57E-04
Naphthalene HAP 6.50E-05 ae 9.66E+00 4.83E-03
Nickel 75 7.20E-05 A 1.07E+01 5.35E-03
o-Xylene HAP 5.80E-05 8.62E+00 4.31E-03
Perchloroethylene of 4.16E-01 2.08E-04
(Tetrachloroethene) 81 2.80E-06
Phenol 82 8.60E-05 Ae 1.28E+01 639E-03
Phosphorus HAP 0.00E+00 0.00E+00
Selenium NA 2.30E-04 h 3.42E+01 1.71 E-02
Styrene 91 2.00E-05 ae 2.97E+00 1.49E-03
Toluene 97 1.60E-04 ae 2.38E+01 1.19E-02
Total Fluorides 50 9.23E-03 a 1,372 6.86E-01
Trichlorofluoromethane 100 0.00E+00 0.00E+00
Vinyl acetate HAP 0.00E+00 0.00E+00
Support Calculations File:General Shale Moneure CY2018 EI 2019-08-11
Printed:W7212019 Page 10 of 34 Sheol:Brick-BH(ES-K4K)NG&Coal

'Emission factors from AP42,Section 11.3,8/97
-Table 11.3-1 for uncontrolled coal-fired and natural gas-fired kilns.
PM for condensible PM= 0.59 lb/ton
abTable 11.3-3 for coal-fired and natural gas-fired kilns.
"Table 11.34 for coal-fired and natural gas-fired kilns
ad Table 11.3-5 for brick kilns.
"Table 11.3-6 for natural gas-fired kilns
'hTable 11.3-7 for natural gas-fired kilns.
"Factor is from AP42 Background Document testing at
Marseilles Brick which has the same type of kiln
Soluble Chromate Compounds is the regulated NC TAP
bEmission factors from AP42,Section 1.4,7/98. The emissions factor in in Ib/mmft3 of gas. The actual gas rate:
Actual Gas Usage= 282,869,760 scf(yr= 282.87 mmft3/yr
` Using AP42 background information,assume that total Fluorides emission factor is 60%of the HF emission factor Also DAQ requires that total fluorides include HF,therefore TF=fluorides+HF(lb/yr).
TF=((0.006 lb/ton*0.60)+0.006 lb/ton)*Brick Production ton/yr
dTesting was performed on Kiln 4 on February 10,2006. Emissions Factors are as follows:
Process weight rate daring test 19.93 ton/hr
,-Highest'Run
s Emtssron'sRate Emission Factor
Pollutan't'; .,, �"Tested,(lb/hn) �(lb/ton) ;„
HF* 7.6 0.381
HCI* 1.16 0.058
PM 2.25 0.113
PM filterable 2.25 0.113
SO2** 0.56 0.029
*Total Fluorides are 60%of HF
**SOz data was from a September 27,2004 engineering test on Kiln 3 with
a process weight rate of: 19.58 tons/hr
GSB tested Kiln 4 on September 22,2015 for PM,HCI'and HF.
Highest Run Production Data 15.6 tons of brick/hr
Emission Factors are as follows:
Average,
Emissroo§:Rate Emission Factor
Pollutant' TestedQti7hr) (lb/ton) .'-
PM 1.6 0.10
HCI. 0.41 2.628E-02
HF 0.09 5.769E-03
Support calculations File:General Shale Moncure CY2018 El 201306-11
., Printed:6/122019 ," Page 11 of 34 Sheet:Brick-SH(ES-K4K)NG a Coal

Title: 2018 Air Emission Inventory
Source ID#: ES-K4131,ES-K4D2,ES-K4D3
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
Source: ES-K4D1,ES-K4D2,ES-K4D3 Brick Dryers 1,2,and 3 on Kiln 4
AERO: G-135
Actual Production: 148,609" Tons/yr
Brick Dryer Fuel: NG/Propane
Annual Annual. "
�� s ' Em�ss>ton Factors(lb/ton fired Em>tss>ton Rate � t Em><ss>on
Pollutantproduced) (ll/yr), Rate(TPY)
y.,PM 0.187 ad 27,790 13.89
- PM-10 0.187 ad 27,790 13.89
PM-2.5 0.187 ad 27,790 13.89
S02
NOx 0.098 as 14,564 7.28
VOC 0.03 ab " 4,458 2.23
CO 0.31 ac 46,069 23.03
Formaldehyde 1.55E-01 b
a Emission factors from AP-42,Section l 1.3,8/97
_ as Table 11.3-3 for brick dryer with supplemental gas burner
ab Table 113=5 for brick dryer.
Table 11.3-5 for brick dryer.
ad Table 1 l.3-1 for brick dryer.
b The formaldehyde emissions from the dryer are included in the kiln calculation.
I
Support Calculations File: General Shale Moncure CY2018 El 2019-06-11
Printed:6l12/2019 Page 12 of 34 Sheet:'Bdck-BH(ES-K4K_G135)(total)

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JI
Title: 2018 Air Emission Inventory
-� Source ID#: ES-Coal-CC
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
Coal Crusher
i
Source: ES-Coal-CC Coal Crusher
Controls: CD-Coal-CC NA
Efficiency: 99.0%
{ Maximum,Production: 0 tpy Did Not Operate in 2018
p [Jncontrolled Annual
Emission t
Em�ss>Ion3Factor Em>tss�on
Pol)utant _ Rate(lb/yr) �
PM 1.10 0.00E+00 0.00E+00
PM-10 1.10 0.00E+00 0.00E+00
PM-2.5 1.10 0.00E+00 0.00E+00
Emission factors from AP-42, Section 12.2,Coke Production,Table 12.2-2, 8/97
I
NOTE: Emission factor given in Section 12.2 is for coal crushing controlled by a cyclone.
An uncontrolled emission factor was developed by assuming the cyclone achieved 90%efficiency.
i
Uncontrolled Factor= 0.11 lb/ton
(1-.90)
1.1 lb/ton
� I
I
~i
Support Calculations File: General Shale Moncure CY2018 El 2019-06-11
Printed:6/12/2019 Page 14 of 34 Sheet: ES-Coal Crusher

n i
I ; Title: 2018 Air Emission Inventory
Source ID#: ES-WFS
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
Wood Fuel/Sawdust System
I� AERO: GR21
Source: ES-WFS Wood Fuel/Sawdust System
Hours of Operation 0 hrs
Wood Fuel/Sawdust System
Control: CD-SD-DCI Dust Collector
Description: Two conveyors,which feed materials to the two screens,are both controlled by a dust collector.
EPN: EP-SD-DC1 Did Not Operate in 2018
Source: ES-SD-SCI 8x8 Screen
ES-SD-SC2 8x8 Screen
I
ES-SD-CV1 Transfer Screw Conveyor
{` ES-SD-CV2 Screen Feed Screw Conveyor
J
Variables: Hours of Operation
Factors:
Exit Concentration= 0.01 gr/dscf
L, Flow Rate for System= 2100 cfm
Bagfilter Efficiency= 99%
(� Emissions Before Control
PM Emissions=Emissions After Control/(1 -Efficiency)
PM Emissions= 18.0 Ib/hr
Emissions After Control
(J PM Emissions=Exit Concentration* I lb/7,000 gr*Flow Rate*60 min/hr
J PNI'Emissions= O:T80 ` l6/lir.
0.00 Ib/yr
AJ
I�
Support Calculations File: General Shale Moncure CY2018 El 2019-06-11
Printed:6/12/2019 Page 15 of 34 Sheet: Controlled New WFS(GR-21)

I� Wood Fuel/Sawdust System
Controls: CD-SD-BV1 Bin Vent Filter
I
Description: Storage silo,which is connected to a bin vent Ater,is used as storage for the product.
I1 �
EPN: EP-SD-BV I
I� Did Not Operate in 2018
Source: ES-SD-SDS Sawdust Silo
Variables: Hours of Operation
Factors:
I� Exit Concentration= 0.01 gr/dscf
Flow Rate for System= 400 cfm
Bagfilter Efficiency= 99%
Emissions Before Control
PM Emissions=Emissions After Control/(1 -Efficiency)
I� PM Emissions= 3.4 lb/hr
Emissions After Control
I-1 I
s' PM Emissions=Exit Concentration* 1 lb/7,000 gr*Flow Rate*60 min/hr
PM Emissions.
I i
I
I�
I�
Support Calculations File: General Shale Moncure CY2016 El 2019-06-11
Printed:6/12/2019 Page 17 of 34 Sheet: Controlled New WFS(GR-21)
U

Title: 2018 Air Emission Inventory
Source ID#: Clay Handling
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
Source: ES-CH Clay Handling Equipment.
1 AERO: G-71
Description: This scenario represents the crushing/grinding/screening/storage operations as they
are currently operating.
EPN: Fugitive
Controls: NA
Factors for Grinding&Screening:
AP-42 Section 11.3,Table 11.3-2
Emission Factor for Grinding and Screening
PM emission factor 0.0250 lb/ton
PM-10 emission factor 0.0023 lb/ton
PM-2.5 emission factor 0.0023 lb/ton
Maximum Process Throughput 200 tph
Actual Raw Material Processed 283,360 tpy
Maximum Hours of Operation 2,024 hrs/yr
Control Efficiency for PM 0 % No Control Devices
,.I)escnpfron .
J
F-PC Primary crusher(clay handling
equipment 200 tph)
F-SS1 &F-SS2
handling equipment 200 tph)
F-HM Hammermill#1 (clay handling
Iequipment 200 tph)1 F-FS 1 -F-FS9
screens(clay handling equipment
F-FC4
n handling equipment 200 tph)
{' F-FC5 Finishing Conveyor#5(clay
handling equipment 200 tph)
NSPS
1
Pollutant
Actual`Emisstois
Name (lbs7yr)-` (tons/yr)
LLL!!! PM 7,084 00 3.54
PM-10 652 0.33
PM-2.5 652 0.33
` Support Calculations
Printed:6/12/2019 PP lations File: General Shale Moncure CY2018 EI 2019-Orr11
IPage 19 of 34 Sheet: Clay Handling(G-71)
L1

2018 Air Emission Inventory General Shale Brick Inc.
Source: Intersite Conveyor Moncure Plant
Source: Conveyor from Cape Fear Plant to
Brickhaven Plant F-C-CFBH
Description: The calculations below quantify emissions from the new inter-site conveyor,which will be installed to
transport material from the reclaim building at the Cape Fear site to the ground storage building at
- the Brickhaven site.
EPN: Fugitive
Controls: NA
Factors for Drop Points
Equations obtained from page 13.2.4-3 of AP-42
E=k(0.0032)[(U/5)^1.3/(M/2)^1.4](I-controleff/100)lb/ton
l - where:E=emission factor(lb/ton)
k=particle size multiplier(dimensionless) '
U=mean wind speed(mph)
M=material moisture content(%)
_J
E=k(0.0032)[(U/5)^1.3/(M/2)^1.4]lb/ton
where:
k= 0.74 for PM-30 microns;
0.35 for PM-10 microns;
6.053 for PM<=2.5 microns;
U= 15 mph
M= 10 % estimated from Table 13.2.4-1 of AP-42
PM<=30 microns:
0.74*0.0032*[(15 mph/5)^1.3/(10/2)^1.4]= 1.04E-03 lb/ton
i
PM—10 microns:
0.35*0.0032*[(15 mph/5)^1.3/(10/2)^1.4]= 4.91E-04 lb/ton
_ PM—2.5 microns:
0.053*0.0032*[(15 mph/5)^1.3/(10/2)^1.4]= 7.43E-05 lb/ton
Basis: All emission sources for the proposed grinding room are listed below.
Control Efficiency for PM 0 % No Control Devices
The following source will be subject to NSPS.
Emissions estimated using the Drop Equations from AP-42
Location `' broils
ID Description
t
From Cape Fear to ES-C Conveyor 283,360
Brickhaven 1
Pollutant Potential Emissions.(per"em�ss�on source)
Name (lbs1yr) (tons/yr> ,
PM 294.05 0.15
PM-10 139.08 0.07
-- PM-2.5 2.1.06. 0.01
C Emissions based on Drop Equations Equations a 200 tph,which is the process weight rate for Brickhaven's
existing Grinding Room.
Support Calculations File: General Shale Moncure CY2018 El 2019-06-11
Printed:6/12/2019 Page 21 of 34 Sheet IntersiteConv(Clay Handling)
1

i
i
SAMPLE CALCULATIONS
Grindine&Screenine Emissions
PM Potential Emissions(lbs/yr)
0.001 lb/ton*283360 tpy* 1 drop= 294.05 Ibs/hr
PM Potential Emissions(tons/yr)
294 /2000lb/ton = 0.15 tons/yr
TOTAL EMISSION CALCULATIONS FOR CLAY HANDLING
II! Pollutant Potential Emissions(per emission source)
I Name (Ibs/yr) (tons/yr)
PM 7378.05 3.69
PM 10 790.81 0.40
PM2.5 672.79 0.34
I
i �
I
I
I
I
I
l
Support Calculations File: General Shale Moncure CY2018 El 2019-06-11
Printed.6/12/2019 page 22 of 34 Sheet: InlersiteConv(Clay Handling)

Title: 2018 Air Emission Inventory
Source ID#: ES-CD-8
Description: Rotary Coatings Dryer
Facility: General-Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
Source: ES-CD-8 Rotary Coatings Dryer
Description: Sand is dried in the rotary coatings dryer
EPN: EP=CD-8
Controls: CD-CDBBF
Variables: Hours of Operation
i ,
Dryer Fuel: Natural Gas with Propane/Air Standby
Dryer Gas Rate(MMBtu/hr)= 0.25 MMBtu/hr
Hours of Operation= 450 hrs
Bagfilter Control Efficiency= 99.9%
Heating Value for Natural Gas= 1020 Btu/ft3
1. Gas Usage(Calculated 1.10294E-01 mmft3/yr
based upon hours of operation)_
Uncontrolled Em ss>on Factor- .Emissions. Emissions,
Pollutant " ° {Ib/mmft3) Ref Rafe(Ib/yr) Rafe(tpy)
r PM 0.52 3 3.11E+00 1.55E-03
j PM-10 0.52 3 3.11E+00 1.55E-03
PM-2.5 0.52 3 3.11E+00 1.55E-03 .
SO2 6.00E-01 I 6.62E-02 3.31E-05
NOx 100 ' 1.10E+01 5.51 E-03
VOCs 5.5 ' 6.07E-01 3.03E-04
CO 84 ' 9.26E+00 4.63E-03
2-Methylnaphthalene 2.40E-05 ' 2.65E-06 1.32E-09
3-Methylchloranthrene 1.80E-06 ' 1.99E-07 9.93E-11
7,12-Dimethylbenz(a)anaihracene 1.60E-05 ' 1.76E-06 8.82E-10
Acenaphthene 1.80E-06 ' 1.99E-07 9.93E-11
Acenaphtylerie 1.80E-06 ' 1.99E-07- 9.93E-11
j„ Acetaldehyde 1.52E-05 2 1.68E-06 8.38E-10
Acrolein 1.80E-05 2 1.99E-06 9.93E-10
- Anthracene 2.40E-06 ' 2.65E-07 1.32E-10
Ammonia 3.20E+00 z 3.53E-01 1.76E-04
Benz(a)anthracene 1.80E-06 ' 1.99E-07 9.93E-11
Benzene 2.10E-03 ' 2.32E-04 1.16E-07
Support Calculations File: General Shale Moncure CY2018 El 2019-06-11
Printed:6/12/2019 Page 24 of 34. Sheet: Dryer(ES-CD-8)

f
s
Benzo(a)pyrene 1.20E-06 ' 1.32E-07 . 6.62E-I1
Benzo(b)fluoranthene 1.80E-06 ' 1.99E-07 9.93E-II
1 Benzo(g,h,I)perylene 1.20E-06 ' 1.32E-07 6.62E-II
Benzo(k)fluoranthene 1.80E-06 ' 1.99E-07 9.93E-I1
Butane 2.1 ' 2.32E-01 1.16E-04
Chrysene - 1.80E-06 ' 1.99E-07 9.93E-II
i - Dibenzo(a,h)anthracene 1.20E-06 ' 1.32E-07 6.62E-II
- Dichlorobenzene 1.20E-03 ' 1.32E-04 6.62E-08
Ethane 3.1 ' 3.42E-01 1.71E-04
Fluoranthene 3.00E-06 ' 3.31E-07 1.65E-10
` Fluorene 2.80E-06 ' 3.09E-07 1.54E-10
1 Formaldehyde 7.50E-02 ' 8.27E-03 4.14E-06
Hexane 1.8 ' 1.99E-01 9.93E-05
Indeno(1,2,3-cd)pyrene 1.80E-06 ' 1.99E-07 9.93E-II
Naphthalene 6.10E-04 ' 6.73E-05 3.36E-08
Pentane 2.6 ' 2.87E-01 1.43E-04
I
Phenanathrene 1.70E-05 I 1.88E706 9.38E-10
Propane L6 ' 1.76E-01 8.82E-05
Pyrene 5.00E-06 I 5.51E-07 2.76E-10
Toluene 3.40E-03 ' 3.75E-04 1.88E-07
Arsenic 0.00E+00 2 O.00E+00 0.00E+00
-- Barium 4.40E-03 ' 4.85E-04 2.43E-07
Beryllium, 0.00E+00 2 0.00E+00 0.00E+00
Cadmium 0.00E+00 2 0.00E+00 0.00E+00
Chromium(as chromic acid) O.00E+00 2 0.00E+00 0.00E+00
Cobalt 8.40E-05 ' 9.26E-06 4.63E-09
Copper 8.50E-04 ' 9.38E-05 4.69E-08
CO2 1.20E+05 2 1.32E+04 6.62E+00
- Lead 5.00E-04 I 5.51 E-05 2.76E-08
Manganese 0.00E+00 2 0.00E+00 0.00E+00
Mercury 0.00E+00 2 0.00E+00 0.00E+00
Methane 2.30E+00 ' 2.54E-01 1.27E-04
Molybdenum l.10E-03 ' 1.21 E-04 6.07E-08
N20 2.20E+00 ' 2.43E-01 1.21E-04
Nickel 0.00E+00 2 0.00E+00 0.00E+00
Selenium 2.40E-05 ' 2.65E-06 1.32E-09
Vanadium 230E-03 I 2.54E-04 1.27E-07
Zinc 2.90E-02 ' 3.20E-03 1.60E-06
I AP 42;Compilation of Air Pollutant Emission FactorsVol. I-Stationary Sources USEPA,
- - 5th ed.Section 1.4,3/98-Small Boilers-Uncontrolled
z NC Department of Air Quality,Natural Gas Spreadsheets-Small Boiler-Uncontrolled
3 PM&PM-10 Emissions were calculated by adding natural gas combustion factors and(NC Spreadsheets
for PM,PM-10 from NEI)and factors for industrial sand dryers(AP-42,Section 11.19)
Support Calculations File: General Shale Moncure CY2018 El 2019-06-11
Printed:6/12/2019 Page 25 of 34 Sheet: Dryer(ES-CD-8)

r
Parameter
Maximum Hourly Coatings Rate 3.45 ton/yr
Actual Annual Coatings Rate 1,552.50 ton/yr
Industrial Sand Dryer Emission
Factor*
2.00 lb/ton
PM/PM-10/PM-2.5 Emissions= 3.45 ton/yr*2 lb/ton
PM/PM-10/PM-2.5 Emissions 6.90 Ib/hr
PM/PM-10/PM-2.5 Emissions= 1552.5 ton/yr*2 lb/ton
- PM/PM-10/PM-2.5 Emissions= 3,105 Ib/yr
Controlled Emissions= 3 lb/yr
* Due to the lack of emission factors for this type of operation,the industrial sand
dryer emission factor from AP-42,Section 11.19 was selected for use. It is felt that
this is a conservative factor because the factor is for mined quartzite that is
processed into sand,which is normally a dirtier operation than is conducted for
coatings at brick plants.
Printed:6112/2019 Support Calculations File: General Shale Moncure CY2018 EI 201M641
Page 26 of 34 Sheet: Dryer(ES-CD-8)

� I
Title: 2018 Air Emission Inventory
Source ID#ES-VS1,-VS2,-VS3,-VS4,&-VS5
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID A 1900009
Vacuum Systems
The vacuum systems,which all connect to a bag filter,are used to collect particulate matter from the empty kiln
cars at both the Brickhaven and Cape Fear Plants. VS-3 is used to remove sand at the sand seal discharge at the
Brickhaven Plant.
FACTORS Exit Concentration= 0.01 gr/dscf
Flow Rate for System= 1400 cf n
Bagfilter Efficiency= 99 9%
G-70 Hours of Operation-Cape Fear= hr/yr
(IES-VS 1)
Hours of Operation-Brick Haven 1,500 hr/yr
(IES-VS2)
Total 1,500 hr/yr
GR-22 Hours of Operation-Brick Haven 2,000 hr/yr
J� (IES-VS3)-Kiln 3 Hi-Vac
Hours of Operation-Brick Haven - hr/yr
(IES-VS4&-VS5)
P J Total 2,000 hr/yr I
Emissions Before Control
1 1 PM Emissions=Emissions After Control/() -Efficiency;
,u+ PM Emissions= 120.0 lb/hr
Emissions After Control
I
PM Emissions=Exit Concentration* I lb/7,000 gr*Flow Rate*60 min/hr*(1-Efficiency.
PM Emissions= 0.120 lb/hr
PM-10 Emissions= 0.120 lb/hr
PM-2.5 Emissions= 0.120 lb/hr
1�
EMISSION CALCULATIONS
Actual Emissions=PM Emissions,Ib1hr(After Control)*Hours of Operation,hr/yr i
G-70(IES-VS1&-VS2)
Pollutant`. Actual Emissions BH Actual Emissions CF., Total Actual.Emissions
Name, lbs('r tons/ r (Ibs/yr) ;:' (tons . ,(tons/yr);
I PM 180.00 0.090 0.00 0.000 180.00 0.090
J PM-10 180.00 0.090 0.00 0.000 180.00 0.090
PM-2.5 180.00 1 0.090 0.00 0.000 180.00 0.090
JG-22(IES-VS3,-VS4&-VS5)
Pollutant Actual Emtssions-VS3 Actual'Emissioits VS4&VSS Total Actual'Emissions,
Name Ibs/:r , tonsl.r {Ibs/yr) (tons/yr) (k4tyr). (tons/yi)".
1 PM 240.00 0.120 0.00 0.000 240.00 0.120
J PM-10 240.00 0.120 0"00 0.000 240.00 0.120
PM-2.5 240.00 0.120 0.00 0.000 240.00 0.120
Support Calculations File: General Shale Moncure CY2018 El 2019-06-11
Printed:6/12/2019 Page 27 of 34 Sheet: Vacuums(GR-22&G-70)

1
Title: 2018 Air Emission Inventory
- Source ID N:ES-BP-FAS -
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility 111 0:1900009 Did Not Operate in 2018.
I _
a� :, " � Controlled Controlled Conhrolled '}x _' � 1' "t f,,, v,•
- Source ,FM PMra
I Emrsslon Classtficatwn Codtrol Emrsawn Emission Emusroo 8i ,; f r
Device ID z as.
Sonrce. It
(SCC) Factor * Fae[or Factor �"'� 77trou- ut� PM Emisstons RM10 Emissions - PMrS Emissrom *s -
,Desert Uon >.(Ibfton). .'i(Ib/66 S 6AE[Num ;• .-r•':(tPY)
_ Flvash Silo 3-05-011-06 binvent 0.0089 0.0049 0.0049 0 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.60E+00 . 0.00E+00
a Controlled PM emission factors for aggregate transfer,pnot m rlic Oyash loading,ime matic loading ofcerrient silo,neigh hopper loading,and mixer loading from AP42,Section -
11.12-Comole Batch Opcmtiom.(10/Ol).
I
Fly
ash k� l
SdoFrlhng
h
FlvasSrlo Emtssions,
'Nazardtius .Emission ,,•„ - ,
Example Calculations:
.�Potlu(ant •i(Ib/[oo) _,O_v'J) ,.':`(iPr)
Arsenic LOOE-06 0.00E+00 0.00E+00 PM Potential Emissions(lbs/yr)
Beryllium 9.04E-08 0.00E+00 0.00E+00 0.009lb/ton•Otpy=ibs/yr 0lbs/yr _
Cadmium 1.98E-08 0.00E+00 0.00E+00 -
'� Chromium 1.22E-0G O.00E+00 0.00E+00- PM potential]Emissions(tons/yr)
--- Lead 5.20E-07 0.00E+00 O.00E+00 0 lbs/yr•(I ton2000 lb)= O.00E+W tons(yr
Manganese 2.56,E-07 0.00E+00 0.00E+00
Nickel - 2.28E-06 O.00E+W 0.00E+00
Phosphor 3.54E-06 0.00E+00 0.00E+00
Selenium 7.24E-08 0.00E+00 0.00E+00
- I
l -
Support Calculations File:General Shale Moncure CY2018 El 2019-06-11
Printed:6/122019 - Page 29 o134 Sheet Flyash Silo -

Tide: 2018 Air Emission Inventory
Source ID H: ES-BP-CS
Facility: General Shale Brick,Inc.
Location: MoncureNC
Facility ID 9:1900009
Did Not Operate in 201E
Controlled Controlled'Source, '�. Fm
Emsston 4' i 2016A I,
ode'tio Device IV;. n
Numbers Th TM Emissions Tactcpr,,�:,:,�',Faiftor
Cement Sil, 3-05-011-07 bin vent 0.00099 0.00034 0.00034 0 0.0013+00 0.00E+00 0.0011+00 0.0013+00 0.0013+00 0.0013+00
a Controlled PM emission factors for aggregate transfer,pneumatic flyash loading,pneumatic loading of cemcni silo,weigh hopper leading,and mixer loading from AP42,Section
11.12-Concrete Batch Operations,(10101).
Cimiiifsilo
Hazardous Emission Cement Silo'.'Em%I
Air Example Calculations:
i.I iu7tli 4 -''(tPY)is -
Arsenic 4.24E-09 0.00E+00 0.00E+00 PM Potential Emissions Ohslyr)
Beryllium 4.86E-10 O.00E+00 0.00E+00 0.00099]b/t...Dtpy-lbs/yr 0 lbs/yr
Cadmium 4+8613-10 0+00E+00 0.0013+00
Chromium 2.90E-07 0.0013+00 0.00-1-00 PM Potential Emissions(lonslyr)
Lead 8 0.0013+00 0.00E-1-00 0 lbs/y,•(I ton/2000 lb)= 0.00E+00 tonslyr
Manganese 1.1 7F-07 0.00E400 0.0011400
Nickel 4.1 8E-05 0.0013+00 0+00E+00
Phosphorus
Selenium
Support Calculations File.General Shale Moneure CY2018 El 2019-06-11
Printed:61120019 Page 30 of 34 Sheet Cement Silo

Title: 2018 Air Emission Inventory
Source ID p: ES-BP-BM
Facility: General Shale Brick,Inc.
Location: Moncore,NC
Facility ID 8: 1900009
Did Not Operate in 2018:
- - Cbntrolled Controlled
source PM '.-PMta I •�
Emission Classificahon Control Emission Emtssron 2016 AEt
j .. Device ID -
Source Code(SCC) Fadot' :Factor Numbers Throughput 4 PM Emissions PM�e:Emissions '( PINu Emissrond"it
•Descri tion .(Iblion).. •;�0611on}'", v'pblton). ;(1P-Y),r;. ....:., .06IY)1 1':�„(tPY), :'. .(Ib/Y).;
Mixer Loading 3-05-011-09 bagfrlter 0.011 0.0038 0.0038 0 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00
a Controlled PM emission favors for aggregate transfer,pneumatic flyash loading,pneumatic loading of cement silo,weigh hopper loading.and mixer loading from AP-12,Section
11.12-Concrete Batch Opcmtions,(10/01).
Batch Mier.
Emission Balch Mrser.Emissrons;,.
Haaardous Air t_Factors Example Calculations:
c Pollutant'"�•'± (Iblton) �`(Ib/Y) `.:�hPY) <<
Arsenic 1.87E-08 0.0000 0.00E+00 PM Potential Emissions(lhs/yr)
Beryllium - - - 0.01llb/lon•01py=lbs/yr 0lbsh•r
Cadmium 7.10E-10 0.0000 0.00E+00
Chromium 1.27E-07 0.0000 0.00E+00 PM Potential Emissions(tons/yr)
- Lead 3.66E-08 0.0000 0.00E+00 0 lbs/yr•(I ton12000 lb)= 0.00E+00lons/yr
Manganese 3.78E-06 0.0000 0.00E+00
-- Nickel 2.48E-07 0.0000 0.00E+00
Phosphorus 1.20E-06 0.0000 0.00E+00
Selenium - -
I -
I
Support Calculations _ File:General Shale Moncure CY2018 El 2019-0&-11
Printed:6112l2019 Page 31 of 34 Sheet Balch Mbrer

Title: 2018 Air Emission Inventory General Shale Brick
Source: ES-RUMBLE Rumbler
Description: Rumbler tumbles blocks in a rotating drum in order to create an "aged" look.
EPN: EP-RUMBLE
Controls: Baghouse CD-RUMBLE Did Not Operate in 2018
Hours of Operation:P 0 hrs
Factors:
- Exit Concentration= 0.01 gr/dscf
Flow Rate for System= 5000 cfm
Bagfilter Efficiency= 95%
Emissions Before Control
PM/PM-10/PM-2.5 Emissions=Emissions After Control/(1 -Efficiency)
PM/PM-10/PM-2.5 Emissions= 8.6 lb/hr
0.0 lb/yr
0.0 tpy
PM/PM-10/PM-2.5 Emissions=Exit Concentration* 1 lb/7,000 gr*Flow Rafe*60 min/hr
PM/PM-10/PM-2.5 Emissions= 0.429 lb/hr
0.00 lb/yr
0.00 tpy
Pollutant. .' '. Ctintrtilled
Actual,Emtssions
Name (lbs%hr) {lbs/yr) (Eons/yr)
PM 4.29E-01 0.00E+00 0.00E+00
PM-10 4.29E-01 0.00E+00 0.00E+00
PM-2.5 4.29E-01 0.00E+00 0.00E+00
Printed.6/12/2019 Support Calculations File: General Shale Moncure CY2018 El 2019-06-11
Page 32 of 34 Sheet: Rumbler

J
1
Title: 2018 Air Emission Inventory
Y SourceTD It: Summary
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Emissions Summary
' Clay
Handling
(Including
Coal Controlled.. 'Intersite Sand Vacuum Cement Storage • Total Total
WFS Conve or Texturing D. er Systems. FI 4sh•Silo Silo Batch Mixer Rumbler Tanks . (lb/yr) (TPY)
Pollutant CAS Number TAP/HAP Brick Crushing y ) g Dryer y y'
JCriteria Pollutants(tons/yr)
PM 1[4
55E+01 0.00E+00 0.00E+00 3.69E+00 2.67E-01 1.55E-03 2.LOE-01 0.00E+00 0.00E+00 0.00E+00 0.00E+00 1.39E+05 69.62
PM-10 55E+01 . 0.00E+00 0.00E+00 3.95E-01 2.67E-01 1.55E-03 2.10E-01 0.00E+00 0.00E+00 0.00E+00 0.00E+00 1..33E+05 66.33
PM2.5 55E+01 0.00E+00 0.00E+00 3.36E-01 2.67E-0I 1.55E-03 2.10E-0I 0.00E+00 0.00E+00 0.00E+00 0.00E+00 1.33E+05 66.27
S02 .50E-01 3.31E-05 - 1.70E+03 0.85
NOx 33E+01 5.51E-03 6.66E+04 = 33.29
VOC 01E+00 3.03E-04 1.23E-01 8.27E+03 4.14
CO 47E+01 4.63E-03 1.69E+OS 84.7I- Deminimus Report
Hazardous Air Pollutants(lbs/yr) (lb/yr) (Y/1)
1,4-dichlorobenzene 106-46-7 36 7.13E+00 1.32E-04 7.13E+00 3.57E-03 1 Rep9>�
_I 2-butanone(MEK) 78-93-3 70 3.276+01 3.27E+01 1.63E-02 100 No
2-methylphenol(cresol) 9548-7 35 0.00E+00 0.00E+00 0.00E+00 l0 No
Acetaldehyde 75-07-0 1.68E-06 1.68E-06 8.38E-10 10 No
Acrolein 107-02-8 1.99E-06 1.99E-06 9.93E-10 10 No
Acrylonitrile 107-13-1 4 0.00E+00 0.00E+00 0.00E+00 10 No
Ammonia 766441-7 3.53E-01 3.53E-01 1.76E-04 too No
Antimony ANTIMONYCPDS HAP 4.01E+00 4.01E+00 2.01E-03 10 No
Arsenic ARSENICCPDS 9 4.61E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 4.61E+00 230E-03 0.01 ; ate (s
Benzene 71-43-2 12 4.31E+02 232E-04 4.31E+02 2.15E-01 1 3Repart �
Benzo(a)pyrene 30-32-8 HAP 1.32E-07 132E-07 6.62E-11 1 No
Beryllium BERYLCPDS 16 6.24E-02 0.00E+00 0.00E+00 0.00E+00 - 6.24E-02 3.12E-05 1 No
Bis(2-ethylhexyl)phthalate;di(2-_I E+02
2.97E+02 1.49E-01
117-81-7 39 2.97
eth Ihex 1) hthalate 10 �`u�ll
Bromomethane(Methyl Bromide) 74-83-9 HAP 0.00E+00 0.00E+00 0.00E+00 I No
Cadmium CADMAJMCPDS 23 2.23E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 2.23E+00 1.11E-03 0.1 95N
Carbon Disulfide 75-15-0 27 6.39E+00 6.39E+00 3.20E-03 10 No
Carbon tetrachloride 56-23-5 28 0.00E+00 0.00E+00 0.00E+00 l No
Chlorine 7782-50-5 29 1.93E+02 1.93E+02 0.10 too r Report ,.
8.47E+01 4.24E-02 10 e�ID
Chloroethane(Ethyl Chororide) 75-00-3 HAP 8.47E+01 .I?
•1 Chloroform 67-66-3 31 0.00E+00 0.00E+00 0.00E+00 too No
Chloromethane(Methly Chloride) 74-87-3 HAP 9.96E+01 9.96E+01 4.98E-02 1 � e $
Chromium CROMCPDS HAP 7.58E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 7.58E+00 3.79E-03 0.01
Cobalt 7440-48-4 HAP 3.12E-01 9.26E-06 3.12E-01 1.56E-04 I No
Diethylphthalate 84-66-2 HAP 3.57E+01 3.57E+01 1.78E-02 not an EI pollutant
Dimethylphthalate 131-11-3 HAP 0.00E+00 O.00E+00 0.00E+00 10 No
Di-a-butylphthalate 84-74-2 HAP 2.08E+01 2,08E+01, 1.04E-02 100 No
Ethylbenzene 100-41-4 HAP 6.54E+00 6:54Et00 3.27E-03 l00 No
Fluorine 7782-41-4 50 0.00E+00 0.00E+00 0.00E+00 10 No
Formaldehyde 50-00-0 51 2.12E+01 9713-03.2 2.12E+01 1.06E-02 10 SO
e ,art
Hexane 110-54-3 HAP - 1.99E-01 1.99E-01 9.93E-05 100 No
0.00E+00 0.00E+00 10 No
Hydrazine 302-01.-2 HAP 0.00E+00 8.57E+02 4.29E-01 100 �� "'o �l
HF 7664-39-3 59 8.57E+02 3.91E+03 1..95E+00 100 :Re`Yrt
HCI 7647-01-0 57 3.91E+03
Hydrogen Sulfide 7783-064 60 0.00E+00 0.00E+00 0.00E+00 1 No
Iodomethane(Methyl Iodide) 74-88-4 HAP 1.38E+01 1.38E+01 6.91E-03 1 IRA
eport
Lead LEADCPDS HAP 2.23E+01 5.51E-05 1 0.00E+00 1 0.00E+00 1 0.00E+00 2.23E+01 r I. lE-02 1 `Re rC
Support Calculations File: General Shale Moncure CY2018 El 2019-06-11
Printed:6%12/2019 Page 33 of 34
Sheet: Summary