AQ_F_1900009_20180702_EI_Cmb-EI-File

2017 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 YES
NO
Initial Review/Data Entry
Q� Enter date received into ED. Date Received:
Assigned to appropriate individual. Date Assigned: Date Due: /e./S.f,�/�
❑ Paper copy submitted: One copy received with supporting documentation,certification form signed by responsible official,and
appears generally complete;OR
iff Electronic copy submitted: All supporting documentation and certification form(with time/date stamp)signed by responsible
official has been received.
Comments:
Inventory Review
❑ All forms and supporting documentation appear to be complete if paper submission(check ED OS data if electronic).
0 Contact,address,phone number changes entered into I-Beam/Facilities if necessary.
0 All known operating scenarios,control devices,and emission release points have been entered for each emission source(permitted,
insignificant,and unpermitted)or note that the emission source was not operated or not required to report.
Check if SCC codes for each OS are accurate and update if needed.
0 Evaluate"U"sources for significance and address according to policy.
0 Calculations/forms appear to add up correctly.
0 All compliance issues are being addressed(e.g.Toxics limits,above TV thresholds,large emissions increase/decrease,installation
without a permit).
0 All volatile HAPs/TAPs were included in the VOC total.
0 Calculations and control efficiencies appear correct. Emission factors are the best available and most current factors appropriate
for the reporting facility(e.g. stack testing,AP-42,etc.).
0 Review facility comments and address any issues.
❑ Update ED(Data Entry Main)if additional information is required(corrections due date and date received).
0 Check all ED QA/QC reports.
0 Comparison with previous emission inventory must be made and outliers(> 10%)must be investigated and explained.
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: A,? • nD/8 Signature: `
Date Submitted to EI Coordinator: $ • Q-QO/B
Date Approved: Initials:

Facility Total CY 2017 Emission Summary Recorded in ED Facility ID#: 1900009
Facility Name: General Shale Brick, Inc. - Moncure Facility Permit#(s): 04384T39
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 emissior No GHGs
times their 1995 IPCC Global Warming Potential (GWP), Reported
converted to metric tons)
Criteria Pollutants Actual Emissions
(Tons/Year)
Pollutant CAS CY 2017 CY 2016 Demini- %
from ED from Fees mus Change
CO CO 82.42 67.68 0.5 F21.8%
NOx NOx 32.39 26.61 0.5 2.1.7%
PM(TSP) TSP 66.78 54.10 0.5 23.4%
PM10 PM10 64.42 52.85 0.5 21.9%
PM2.5 PM2.5 64.38 52.83 0.5 21.9%
S02 SO2 0.830000 0.680000 0.5 22.1.%
VOC VOC 4.57 3.88 0.5 17.8%
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPs) (Pounds/Year)
Pollutant CAS CY 2017 CY 2016 Demini- %
from ED from Fees mus Change
Arsenic& Compounds(total mass of elemental AS, arsine and 4.49 3.68 0.01 1220%
all inorganic compounds)
Arsenic Unlisted Compounds- Specify Compound ASC-Other 4.49 3.68 0.01 22.1%
(Component of ASC)
Cadmium &compounds(total mass includes elemental metal) 2.17 1.78 0.1 121.9%
Cadmium Metal, elemental, unreacted(Component( 7440-43-9 2.17 1.78 0.1 22.1%
CDC)
Chromium-AIUTotal(includes Chromium (VI) categories, 7.39 6.05 0.1 122.1%
metal and others)
Chromic acid (VI) (Component of So1CR6 & CRC) 7738-94-5 7.39 6.05 0.01 122.1%
Chromium (VI)Soluble Chromate Compounds(Component of 7.39 6.05 0.01 122.1%
CRC)
08/02/2018 Page 1 of 3

Facility Total CY 2017 Emission Summary Recorded in ED Facility H)#: 1900009
Facility Name: General Shale Brick, Inc. -Moncure Facility Permit#(s): 04384T39
Hazardous Air Pollutants (HA-Ps) Actual Emissions
and/or Toxic Air Pollutants (TAPs) (Pounds/Year)
Pollutant CAS CY 2017 CY 2016 Demini- %
from ED from Fees mus Change
Chromic acid(VI) (Component of So1CR6 & CRC) 7738-94-5 7.39 6.05 0.01 22.1.%
Lead& compounds 21.75 17.81 1.0 22.1%
Lead Unlisted Compounds- Specify Compound PBC-Other 21.75 17.81 10.0 22.1'%
(Component of PBC)
Mercury & Compounds-all total mass includes Hg Vapor 1.09 0.890440 0.001 22.4%
Mercury, vapor(Component of HGC) 7439-97-6 1.09 0.890440 0.001 22.1%
Nickel& Compounds,sum total mass includes elemental 10.44 8.55 1.0 22.1%
Nickel metal (Component ofNIC) 7440-02-0 10.44 8.55 1.0 22.1%
Polycyclic Organic Matter(Specific Compounds from OAQPS 9.42 7.72 1,0 22.0%
for T iq
Naphthalene (Component of 83329/POMTV) 91-20-3 9.42 7.72 1.0 22.1%
Benzene 71-43-2 420.47 344.30 1.0 22.1%
Chlorine 7782-50-5 188.49 154.34 100.0 22.1%
DEHP(Di(2-ethylhexyl)phthalate) 117-81-7 289.98 237.45 10.0 22.1%
Dichlorobenzene(p), 1,4- 106-46-7 6.96 5.70 1.0 22.10/0
Ethyl chloride (chloroethane) 75-00-3 82.64 67.67 10.0 22.1%
Fluorides (sum of all fluoride compounds as mass of 16984-48-8 2,319.84 1,899.60 10.0 22.1%
ion)
Formaldehyde 50-00-0 23.91 19.62 10.0 21.9%
Hexane, n- 110-54-3 0.198530 0.459000 100.0 1-56.7%
Hydrogen chloride (hydrochloric acid) 7647-01-0 4,349.70 3,561.75 100.0 22.1%
Hydrogen fluoride (hydrofluoric acid as mass of HF) 7664-39-3 1,449.90 1,187.25 100.0 22.1%
(Component of 16984488/Fluorides)
Methyl chloride (chloromethane) 74-87-3 97.14 79.55 1.0 22.1%
Methyl iodide (iodomethane) 74-88-4 13.48 11.04 10.0 22.1%
Selenium Compounds SEC 33.35 27.31 10.0 22.10%
Styrene 100-42-5 2.90 2.37 100.0
08/02/2018 Page 2 of 3

Facility Total CY 2017 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 2017 CY 2016 Demini- %
from ED from Fees mus Change
Toluene 108-88-3 23.20 19.00 100.0 22.1
Largest Individual HAP Hydrogen chloride(hydrochloric acid) 4,349.70 lbs
Total HAP Emissions 7,039.09 lbs
Largest Individual CAP CO 82.42 tons
Total CAP Emissions 184.63 tons
Total TAP Emissions 9,096.64 lbs
Total Aggregate 188.78 tons
Emissions
DAQ's Comments Regarding Inventory
Brick production for 2017 was up 22.1 percent from the brick production in 2016 and that accounts for the vast majority of percent
change for the pollutants emitted in 2017. The percent change in Hexane,n-is due to the rotary sand dryer operation where the less
than 0.2 pounds emission this year compared to the less than 0.5 pounds emission last year for a pollutant that has a deminimus
value of 100 pounds.
08/02/2018 Page 3 of 3

Williams, Stanley
From: Warren Paschal <[e-mail]>
Sent: Wednesday,August 01, 2018 3:42 PM
To: Williams, Stanley
Cc: [e-mail]
Subject: RE: [External] RE: 2017 Emission Inventory
Nw
k �z.
Okay,thanks.
Warren Paschal
Manager of Environmental Compliance
General Shale I www.generalshale.com
300 Brick Plant Road
Moncure,NC 27559
Office:[phone](Ext.221)Cell:[phone]
warren.paschalageneralshale.com
From:Williams,Stanley<[e-mail]>
Sent:Wednesday,August 01, 2018 3:29 PM
To:Warren Paschal<[e-mail]>
Subject: RE: [External] RE: 2017 Emission Inventory
That will not be necessary, l can simply correct the number and it will make a slight difference. The correction will apply
to the kiln, the kiln dryer, and the texturizing because all those OS's used the 144,454 tons. Let me know if you have any
questions.
From:Warren Paschal [mailto:[e-mail]]
Sent:Wednesday,August 01, 2018 3:03 PM
To:Williams,Stanley<[e-mail]>
Cc:[e-mail]
Subject: [External] RE: 2017 Emission Inventory
• o. . 11 . Mlillllgl lig . . iiiiiiiio
fi tsrEt 5 m
Thanks Stan. My error. It should have been 144,990 tons.Should we submit a revision?
Warren Paschal
Manager of Environmental Compliance.
General Shale I www._qeneralshale.com
300 Brick Plant Road
Moncure, NC 27559
Office:[phone](Ext.221)Cell:[phone]
warren.paschal na generalshale.com
1

From:Williams,Stanley<[e-mail]>
Sent:Wednesday,August 01,2018 10:18 AM
To:Warren Paschal<[e-mail]>
Cc: [e-mail]
Subject: 2017 Emission Inventory
Warren,
I have started my review of your 2017 emission inventory submittal(HERO)and there seems to be a discrepancy in the
throughput for Kiln 4. The facility had reported via the quarterly reports that for calendar year 2017 this kiln had a
throughput of 144,990 tons but in AERO the throughput is shown as 1441454 tons. I know it is not a large difference but 1
just wanted the number to be accurate. This could also affect the texturizing operations(OS-37)throughput as
well. Look forward to your response. Thanks.
.Stag ZMuw, Environmental Engineer
Raleigh Regional Office
NC DEQ, Division of Air Quality
3800 Barrett Drive, Raleigh, NC 27609
Voice:919-791-4200 Fax:[phone]
www.ncair.org
e-mail:[e-mail]
E-mail correspondence to and from this address may be subject to the North Carolina Public Records Law and may be
disclosed to third parties unless the content is exempt by statute or other regulation.
2

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.......................................................................................................................................................................................................
2017 CALENDAR YEAR EMISSIONS INVENTORY
General Shale Brick, Inc. - Moncure, NC Facility
General Shale Brick
Building The American Dream'
N
C Dept of Environmental ouality
�u� 0�2018
pen low 2-M"" gWW
galeigh Regional Office
June 2018
Project 183401.0091
Prepared By:
TRINITY CONSULTANTS
One Copley Parkway
Suite 205
Morrisville,NC 27560
[phone]
Tin n. i t
Consli 4tits
Environmental solutions delivered uncommonly well

TABLE OF CONTENTS
SECTION 1: NCDAQ CY 2017 EMISSION INVENTORY AERO FORMS PAGE
CertificationForm.....................................................................................................................................................................................1
Listing of Emission Sources&Control Devices on Permit.........................................................................................................2
Emission Source&Operating Scenario List....................................................................................................................................9
BrickDryers for Kiln 3 at Brickhaven............................................................................................................................................11
WoodFuel/Sawdust System...............................................................................................................................................................13
VacuumSystem-Brickhaven............................................................................................................................................................16
BrickProcessing-Cape Fear.............................................................................................................................................................18
BrickTexturing.......................................................................................................................................................................................21
VacuumSystem.......................................................................................................................................................................................23
ClayHandling...........................................................................................................................................................................................25
Dryersfor Cape Fear(should be removed)..................................................................................................................................27
BrickDryers-Kiln 4.............................................................................................................................................................................29
StorageTanks..........................................................................................................................................................................................31
BatchMixer...............................................................................................................................................................................................33
CementSilo...............................................................................................................................................................................................35
FlyashSilo.................................................................................................................................................................................................37
CoatingsDryer.........................................................................................................................................................................................39
CoalCrusher.............................................................................................................................................................................................42
Brick Processing-Brickhaven Kiln 3...............................................................................................................................................44
BrickProcessing-Brickhaven Kiln 3...............................................................................................................................................46
BrickProcessing-Kiln 4.....................................................................................................................................................................48
Rumbler.....................................................................................................................................................................................................51
PropaneVaporizer.................................................................................................................................................................................53
FacilityTotals..........................................................................................................................................................................................55
Comments.................................................................................................................................................................................................57
SECTION 2: SUPPORTING EMISSION CALCULATIONS
CriticalParameters...................................................................................................................................................................................1
BrickProcessing-Cape Fear..................................................................................................................................................................2
Brick Processing at Brickhaven Kiln 3 (Firing Coal and NG)....................................................................................................3
BrickDryers at Brickhaven Kiln 3......................................................................................................................................................8
Brick Processing at Brickhaven Kiln 4(Natural Gas/Coal).......................................................................................................9
BrickDryers at Brickhaven-Kiln 4................................................................................................................................................12
BrickSummary.......................................................................................................................................................................................14
CoalCrusher ............................................................................................................................................................................................15
General Shale Brick, Inc. - Moncure, NC Facility I CY 2017 Emissions Inventory
Trinity Consultants

f
WoodFuel/Sawdust.System(New) ...................... ......................................................................................................... ......16
ClayHandling Equipment....................................................................................................................................................................20
IntersiteConveyer.................................................................................................................................................................................21
BrickTexturing.......................................................................................................................................................................................23
CoatingsDryer.........................................................................................................................................................................................24
VacuumSystem.......................................................................................................................................................................................28
StorageTanks..........................................................................................................................................................................................29
i
FlyashSilo.................................................................................................................................................................................................30
CementSilo...............................................................................................................................................................................................31
BatchMixer...............................................................................................................................................................................................32
Rumbler.....................................................................................................................................................................................................33
Summaryof Emissions.........................................................................................................................................................................34
FugitiveSources......................................................................................................................................................................................36
I
f
1
i
_ S
General Shale Brick, Inc. -Moncure, NC Facility I CY 2017 Emissions Inventory
Trinity Consultants

SECTION 1
NCDAQ CY 2017 EMISSION INVENTORY (AERO) FORMS
General Shale Brick, Inc. - Moncure, NC Facility I CY 2017 Emissions Inventory
Trinity Consultants

COPY of RECORD Date Submitted: 6/18/2018 16:24:17
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 2017
These for►ns must be completed and returned even if the facility did not operate or emissions �rere zero
The legally defined "Responsible Official" of record for your facility is Kevin Hain
F_ 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:
(Importanta Legally Resl2gnaible Official. read and sign
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
nalities of up to$25,000 per occurrence and possible imprisonment as outlined in G.S.§143-215.3(a)(2))
Responsible Official's Si naturr BeIM� (use blue ink): Date Signed:
Printed Name: Kevi Ham
Si nature:
This form applies to Title V facilities. If this facility is not classified as Title V,please telephone your regional office Emission
Inventory contact at once for proper forms.
e t of F,nvironmentatQ��
.NC P p
Email address of Responsible Official: [e-mail] '��:101�
r
Information on this Form cannot be held confidential yid
COPY of RECORD Date Submitted: 6/18/2018 16:24:17 1

COPY ®f RECORD Date Submitted: /°i /2 1 :2 :17
s 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
i
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
ES—BP—BM Batch mixer(39.97 tons per CS-12 one bagfilter(535 sgaure CD—BP—BH1
hour capacity) feet of filter area),
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(11 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
Texturizing operation for Line square feet of filter CD—CR6BF, CD—CR7BF1,
ES—CR5 1 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
Texturizing operation for Line square feet of filter CD—CR6BF, CD—CR7BF1,
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),Bagfitter(6,096
Texturizing operation for square feet of filter CD—CR6BF, CD—CR7BF1,
- ES—CR7 CS-19 area),bagfilter(4,062 square
Lines 3 and 4 CD—CR7BF2, CD—CR7BF3
feet of filter area),bagfilter
(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
- of4.7 to 1),
ES—K1 Wood/natural gas—fired.tunnel CS-8 Two Simple cyclones (89 CD—Cl, CD—C2
brick kiln(20.3 million Btu inches in diameter)
2

per hour heat input and 13.7
tons per,hour fired brick
r production rate) [2D .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—Cl, 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— CS-15 dry limestone adsorber, CD—K3DLA
Coal/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]
Natural gas/propane—fired
ES—K4D1 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) [2D .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) [2D .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 CD—Cl, CD—C2
' heat from kilns 1 and 2 with inches in diameter)
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 CD—SD—DC1, CD—SD—DC2,
ES—WFS—SD—CV 1 Transfer screw conveyor CS-17 in di to 1),cyclone
n e vent n inches filter(air CD—WFS—SD—CYC,
n diameter),bin 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—DC 1, CD—SD—DC2,
ES—WFS—SD—CV2 Screen feed screw conveyor CS-17 8.06 to 1),cyclone (42 inches 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—CV3 Enclosed conveyor CS-17 8.06 to 1),cyclone (42 inches 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—DC I, CD—SD—DC2,
W ES— FS—SD—CYC Cyclone CS-17 8.06 to 1),cyclone(42 inches 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—HM Hammermill CS-17 8.06 to 1),cyclone (42 inches 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),
4

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—SC1 8x8 screen CS-17 8.06 to 1),cyclone (42 inches 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—DCI, CD—SD—DC2,
ES—WFS—SD—SC2 8x8 screen CS-17 8.06 to 1),cyclone(42 inches CD—WFS—SD—CYC,
in diameter),bin vent filter(air CD—SD—BVl, 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—SDS Sawdust silo CS-17 8.06 to 1),cyclone(42 inches 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—SH Surge hopper CS-17 8.06 to 1),cyclone(42 inches 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),
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 0001
F—CH—FS 1 Finishing screen [NSPS 000]
F—CH—FS2 Finishing screen[NSPS 000]
F—CH—FS3 Finishing Screen [NSPS
000]
F—CH—FS4 Finishing screen [NSPS 000]
F—CH—H1 Hammermill [NSPS 000]
F—CH—H2 Hammermill [NSPS 000]
F—CH—HFC1 Hammermill Feed Conveyor
[NSPS 000]
5

F—CH—HFC2 Hammermill Feed Conveyor
[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—TC 1 Trampolin Conveyor[NSPS
000]
F—CH—TC2 Trampolin Conveyor [NSPS
f 000]
F—FC4 Finishing conveyor#4 [NSPS
000]
F—FCS 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—FS5 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—SS 1 1
IScalping Screen [NSPS 000]
6

F—SS2 Scalping Screen [NSPS 000]
I—ES—K1D1 brick dryer associated with
Kiln 1
I—ES—K2D1 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—Cl 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
IES—T1 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
IS-14.15A propane vaporizer(1.3 million
Btu per hour per burner)
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 Kiln 3 conveyor
8

COPY f RECORD Date Submitted: /1 / 01 16:2 :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
Emission Source & Operating Scenario List - See Instructions
DES Group ID *ES ID SOS ID *OS Description
GR12 ES-K3D1,ES-K3D2,ES-K3D3 20 Natural gas/propane-fired dryers
for Kiln 3
ES-WFS-SD-CV 1,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
G-66 ES-Kl,ES-K2,ES-WD1,2 14 Wood/natural gas-fired brick kilns
and green brick dryer(Cape Fear)
G-69 ES-CR5,ES-CR6,ES-CR7 37 Texturizing Operations
G-70 IES-VS1,IES-VS2 34 Vacuum System
F-C-CFBH,F-FC4,F-FC5,F-FS2,
F-FS3,F-FS4,F-FS5,F-FS6,F-FS7, Primary Clay Grinding and
G-71 F-FS8,F-FS9,F-PC,F-SS1,F-SS2, 31 Screening Operation
F-FS1
G-72 I-ES-K1D1, I-ES-K21)1 15 Dryers associated with Kilns 1 and
2
F-CH-BC,F-CH-C1,F-CH-CFC,.
F-CH-FC,F-CH-FS1,F-CH-FS2,
F-CH-FS3,F-CH-FS4,F-CH-H1,
F-CH-H2,F-CH-HFC I,F-CH-HFC2,
G-132 F-CH-P1,F-CH-P2,F-CH-RC, NONE NONE
F-CH-SFC1,F-CH-SFC2,F-CH-SFC3,
F-CH-SFC4,F-CH-SSI,F-CH-SS2,
F-CH-SSFC,F-CH-TI,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-CO-2,
IES-F-CO-C1,IES-F-CO-C2,
IES-F-CO-C3,IES-F-CO-C4,
IES-F-CO-05,IES-K4F.1,IES-K417.2,
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,
9

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, 18 Storage tanks
IES—T5
ES—BP—BM 26 Batch Mixer
ES—BP—CS 27 Cement Silo
ES—BP—FAS 28 Flyash Silo
Rotary sand drum dryer(3.45 tons
ES—CD-8 6 per hour)
ES—CR8 NONE NONE
ES—Coal—CC 33 Coal Processing System
10 Natural gas/propane—fired kiln#3
ES—K3K (Uncontrolled)
25 10/Natural gas/propane/coal—fired
kiln#3
Coal/Natural gas/Propane—fired
ES—K4K 21 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—SD NONE NONE
IS-14.15A 19 Propane Vaporizer
10

COPY of RECORD Date Submitted: / / : :1
s entered in
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 2017
1. Emission Source ID (from permit)or Group GR12 consisting of ES—K3Dl,ES—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/Briek Manufacture—Dryer; Brick Dryer: Heated With Waste Heat
And Supplemental Gas Burners
5. Throughput/units in 2017:
(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#): (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—K3Dl AND
ES—K3D2
11

Operating Scenario: OS—20 Emission Source/Group ID: GR12
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2017)
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%
2017 2017 2017 2017
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
2017
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAAQS) Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instnictions) all controls)
2017
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 EF Control
(see instructions) Method Code Efficiency Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2017
12

COPY of RECORD Date Submitted: / / e
As entered in
i
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 2017
1. Emission Source ED(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
E Transferring
j 5. Throughput/units in 2017: 0
(e.g.production or fuel use):
6. Fuel Information (If fuel is used] Sulfur 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—H) CD ID Control Device Description
as listed inpermit)
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 vent filter 4.44:1 air to cloth ratio
J 5 CS-17 CD—SD—BV2 One bin vent filter 4.44:1 air to cloth ratio
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter#): (F)- (Feet/sec) Rate(Acfm)
Rectangle(L x W)
(in 0.1 feet)
13

P—SD—BV1 VERTICAL STACK 20 0.5 72 33.95 400 Bin vent on sawdust
silo
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
Conveyors
14

Operating Scenario: OS—30 Emission Source/Group ID: GR21
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2017)
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% �March—May o une—Aug. o Sept.—Nov. 25%
2017 17 25/0 2017 25/0 2017
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
2017
Criteria Emissions— Emission Control
NAA S Pollutant Criteria Estimation Efficiency Emission
( Q ) Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2017
CO CO 08 0
NOx NOx 08 0
TSP TSP 08 0
PM10 PM10 08 0
PM2.5 PM2.5 08 0
S02 S02 08 0
VOC VOC 08 0
HAP/TAP CAS Emissions Emission Control
Pollutants (In HAP/TAPS Estimation Efficiency Emission EF Control
(see instnictions) Method Code y Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2017
15

i
COPY Of RECORD ®ate Submitted: 6/16/2016 16: :17
s 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 2017
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
i
3. Operating Scenario ID/Description: OS—35/Vacuum Systems—Brickhaven
4. SCC Number/Description: 30500317Brick Manufacture—Material Prep ;Raw Material Unloading
5. Throughput/units in 2017: 2000 HR/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
(Btu/units) .
4
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point RP Information: Sources vented to more than one ERP use additional entry Hues):
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 0.1 feet)
EP—VS3 DOWNWARD—FACING VENT 1 3 72 3.3 1400 Emission Point fot
IES—VS3
EP—VS4 DOWNWARD—FACING VENT 1 3 72 3.3 1400 Emissions point
for IES—VS4
EP—VS5 DOWNWARD—FACING VENT 1 3 72 3.3 1400 Emission
point foi
IES—VS5
F
r.
16

Operating Scenario: OS—35 Emission Source/Group ID: GR22
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2017)
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 25a�o une—Aug. 25%u Sept.—Nov. 25%
2017 2017 2017 2017
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
2017
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission Ef Control
Pollut aantnts y
(NAA Code Pollutants Method Code (Net after Factor
(Tons/Year) (See Instructions) all controls)
2017
CO CO 08
NOx NOx 08
TSP TSP 0.12 08
PM10 PM10 0.12 08
PM2.5 PM2.5 0.12 08
S02 S02 08
VOC VOC 08
Emission
HAP/TAP CAS Emissions Control
Estimation Emission
Pollutants (In (see instructions) HAP/TAPS Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) See Instructions) et after all controls)
2017
17

D i D
COPY of RECORDto Submitted: /16/2018 16:24:17
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 2017
1. Emission Source ID (from permit) or Group G-66 consisting of ES—Kl,ES—K2,ES—WD1,2
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 2017: 0
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) % Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information :
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-8 CD—Cl Simple cyclone 89 inches in diameter .
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/sec) Rate(Aefm)
Rectangle(L x W)
in 0.1 feet)
ERP for ES—K1,
EP—Cl 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 2017)
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% arch—May 250/u une=Aug. 25% Sept.—Nov. 25%
2017 2017 2017 2017 _T
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS y GHG Estimation Efficient Emission
Pollutants Pollutants Method Code (Net after Factor Ef Control
Tons/Year See Instructions all controls
2017
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)
2017
CO CO 08 0
NOx NOx 08 0
TSP TSP 08 0
PM10 PM10 08 0
PM15 PM2.5 08 0
S02 S02- 08 0
VOC 'VOC 08 0
HAP/TAP Emissions Emission Control
CAS. HAP/TAPS Estimation Emission
Pollutants (In
see instructions Efficiency EF Control
( ) Method Code Factor
Alphabetical Order) (Pounds/Year) tructions (Net after all controls)
See Ins
2017
20

COPY of RECORD Date Submitted: /16/2 16: :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 2017
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: 30500397/Brick Manufacture; *Other Not Classified
14q�ag0 em�.�� �ati�l S crr��er�� pow
5. Throughput/units in 2017: -144454 TON/yr -74e- j-K-
(e.g. production or fuel use): k5 f Roos
6. Fuel Information (if fuel is used) %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-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-CR7BF2 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#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
(in 0.1 feet)
EP—CR6 HORIZONTAL STACK 20 1 72 21.2 999.02 ERP for ES—CR-6
EP—CR7 1HORIZONTAL STACKI 20 1 1 72 21.2 999.02 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 2017)
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 �017
ept.—Nov. 25%
2017 2017 2017
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
2017
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficienty Emission
(NAA Code Pollutants Method Code (Net after • Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2017
CO CO 08 0
NOx NOx 08 0
TSP TSP 0.26 08 99 0.0036 AFTER
PM10 PM10 0.26 08 99 0.0036 AFTER
PM2.5 PM2.5 0.26 08 99 0.0036 AFTER
SO2 SO2 08 0
VOC VOC 08 0
HAP/TAP Emissions Emission Control
Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2017
t
r
22

COPY of RECORD Date Submitted: 1 / : 7
As n' r 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 2017
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: 30500317Brick Manufacture—Material Prep ;Raw Material Unloading
5. Throughput/units.in 2017: 1500 HR/yr
(e.g.production or fuel use):
6. Fuel Information. (If fuel is used) /o Sulfur %Ash Heat Content
Btu/units F-1
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 entry lines):
ERP ID ERP Type' Height Diameter Temperature Velocity Volume Flow ERP
(in feet) Circle(enter#): (F). (Feet/sec) Rate(Acfm) Description
ectangle,(L x
) '
(in 0.1 feet)
EPVS2 DOWNWARD—FACING VENT 1 3 72 3.3 1400 ERP for
CD—VS2
EPVS1 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 2017)
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% 25%25% Sept.—Nov., 25%
2017 017 2017 2017
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
2017
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)
2017
CO CO 08 0
NOx NOx 08 0
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 S62 08 0
VOC ,VOC 08 0
HAP/TAP CAS Emissions Emission Control
Estimation Emission
Pollutants (In (see instructions) HAP/TAPS Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2017
1
24

i
COPY of RECORD Date Submitted: l
As entered in AERO
Facility Name: General Shale Brick,Inc.—Moncure Facility Facility ID : 1900009
306 Brick Plant Road Permit : 04384
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
r
Division of Air Quality
Air Pollutant Point Source Emissions Inventory-Calendar Year 2017
1. Emission Source ID (from permit)or Group G-71 consisting of F—C—CFBH,F—FC4,F—FCS,F—FS2,F—FS3,
._ Emission Source Group ID . F—FS4,F—FS5,F—FS6,F—FS7,F-FS8,F—FS9,F—PC,F—SS1,F—SS2,F—FS1
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 2017: 202400 TON/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) % Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP. Information: Sources vented to more than one ERP use additional entry lines
ERP ID 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
STACK) sources
25

Operating Scenario: OS—31 Emission Source/Group ID: G-71
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2017)
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 250�o une—Aug. 250�o Sept.—Nov. 25%
2017 2017 2017 2017
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
2017
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)
2017
CO CO 08
NOx NOx 08
TSP TSP �-5T 2.6F 08 0.021004
PM10 PM10 ,Q:2,'®,Z.3 08 1
PM2.5 PM2.5 0�23 ®,t4. 08 D,oop-s'74
S02 S02 08
VOC VOC 08
HAP/TAP CAS Emissions Emission Control
Pollutants (In HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2017
26

P10 00-r opee �
COPY Of RECORD Date Submitted: /1 / 01 : :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 2017
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 2017: 0
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) %Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) (Acfm)
Rectangle(L x W)
(in 0.1 feet)
EP—FG FUGITIVE(NO 1 72 Area— 1 ERP for Fugitive
STACK) sources
I '
27

Operating Scenario: OS— 15 Emission Source/Group ID: G-72
10.Operating;Schedule: (Source/Operating Scenario that best characterizes Calendar-Year 2017)
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%
2017 017 2017 2017
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
2017
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
- (NAAQS) Code . Y Ef Control
Pollutants Pollutants Method Code (Net after Factor
(Tons/Year) (See Instructions) all controls)
2017
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP Emissions Emission Control
Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2017
28

COPY 0f RECORD to Submitted: /1 12O1 16: :17
s 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 2017
1. Emission Source ID (from permit) or Group G-135 consisting of ES—K4Dl,ES—K4D2,ES—K4D3
Emission Source Group ID
2. Emission Source Description: Natural gas/propane—fired dryers at Brickhaven Plant
F 3. Operating Scenario ID/Description: OS—29/Natural gas/propane—fired dryers for Kiln 4
4. SCC Number/Description: 30500351Brick Manufacture—Dryer;Brick Dryer: Heated With Waste Heat
And Supplemental Gas Burners
144,61tcl o
5. Throughput/units in 2017: JA TON/yr (144`61 6?0 ravo
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) % Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
-- 9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
(in 0.1 feet)
EP—K4D1 VERTICAL STACK 34.78 4.92 99.95 33.79 38544.24 Brick Dryers on
_ Kiln 4
29

Operating Scenario: OS-29 Emission Source/Group ID: G-135
-{ 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2017)
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
12. Seasonal Periods Percent Annual Throu h ut:
an-Feb +Dec 25% arch-May 25% une-Aug. 25% Sept.-Nov. 25%
2017 2017 2017 017
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
Pollutants CAS Pollutants Method Code (Net after Factor Ef Control
Tons/Year See Instructions all controls
2017
Criteria Emissions- Emission Control
Pollutant Criteria, Estimation' Efficiency Emission
(NAAant Code Pollutants Method Code (Net after Factor Ef Control
Pollutants -
(Tons/Year) :(See Instructions) all controls)
2017
CO CO 22. 08 0.31
NOx NOx 1-W-IJO 08 0.098
TSP TSP 13..A64 08 0..187
PM10 PM10 13.545e 08 0.187
PM2.5 PM2.5 13. 54, 08 0.187 .
S02 . S02 -08-
VOC VOC 2.17 08 0.03
- HAP/TAP CAS Emissions Emission Control
Pollutants (In HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Factor
-' Alphabetical Order), (Pounds/Year) Method Code (Net after all controls)
See Instructions
2017
30

COPY of RECORDto Submitted: /18/20181 : :17
s 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 2017
1. Emission Source ID (from permit) or Group G-144 consisting of IES—Tl, 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 2017: 81935 GAL/yr
(e.g. production or fuel use):
6. Fuel Information (If fuel is used) % Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional 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
31

Operating Scenario: OS— 18 Emission Source/Group ID: G-144
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2017)
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 o une—Aug. o Sept.—Nov.
2017 25/0 �arch—May
17 25/0 2017 25/0 017 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
2017
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)
2017
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 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)
2017
i
32

F 3
COPY of RECORD Date Submitted: /18/201016:2 :17
s 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 2017
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—26/Batch Mixer
4. SCC Number/Description: 31299999/Miscellaneous Machinery ; Other Not Classified
5. Throughput/units in 2017: 0
(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 100
Device or Stack):
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-12 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 ft (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
-I 10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2017)
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%
2017 2017 2017 2017
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
2017
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)
2017
CO CO 08 0
NOx NOx 08 0
TSP TSP 08 0
PM10 PM10 08 0
PM2.5 PM2.5 08 0
S02 S02 - 08 0
VOC VOC 08 0
Emission
HAP/TAP CAS . Emissions Estimation Control Emission
Pollutants (In (see instructions) Method.C HAP/TAPS ode Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2017
i
I
34

ID i0 No--r Ofte?
COPY of RECORD Date Submitted: 1
As entered in AERO
Facility Name: General Shale Brick, Inca—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 2017
1. 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 2017: 0
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) % Sulfur I Ash I I 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-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#): (F) (Feet/see) Rate(Acfm)
Rectangle(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 2017)
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�0 arch—May 250�0 une—Aug. 25% Sept.—Nov. 25%
2017 2017 2017 2017
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
2017
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)
2017
CO CO 08 0
NOx NOx :08 0
TSP TSP 08 0
PM10 PM10 08 0
PM2.5 PM2.5 08 0
S02 S02 08 0
VOC VOC 08 0
HAP/TAP Emissions Emission Control
Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) See Instructions) (Net after all controls)
2017
i
36

010 NOT
COPY of RECORD Date Submitted: 6/18/2018 -16:24:17
,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 2017
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 2017: 0
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) % Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 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 ft (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 2017)
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 2 % une—Aug. 250% ISept.—Nov. 25%
2017 2017 2017 2017'
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
Pollutants CAS Pollutants Method Code (Net after Factor Ef Control
Tons/Year See Instructions all controls
2017
Criteria Emissions— Emission Control
Pollutant. Criteria Estimation ,Efficiency Emission
(NAAn Code Pollutants Method Code (Net after Factor Ef Control
Pollutants t
(Tons/Year)- (See Instructions) all controls)
2017
CO CO 08 0
NOx NOx 08 0
TSP TSP 08 0
PM10 PM10 08 0
PM2.5 PM23 08 0
S02 S02 08 0
VOC VOC 08 0'
' 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)
2017
38

COPY of RECORD Date u / /
As entered. s
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 2017
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;
r 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: 30500301/Brick Manufacture—Dryer;Raw Material Drying
5. Throughput/units in 2017: 0.110294 E6FT3/yr .
(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)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter _ Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter#): (F) (Feet/see) (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 2017)
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%
' 017 1 2017 2017 2017
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
2017
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)
2017
CO CO 0 08 84
NOx NOx 0.01 08 100
TSP TSP 0 08
PM10 PM10 0 08
PM2.5 PM2.5 0 08
S02 S02 '08
VOC VOC 08
Emissions Emission Control
HAP/TAP CAS Emission
HAP/TAPS Estimation, Efficiency EF Control
Pollutants (In Alphabetical Order) (see instructions) Method Code (Net after all Factor
(Pounds/Year)
See Instructions controls)
2017
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
(Specify and Component of PBC—Other 0.00006 08 0.0005 ✓
PBC
Naphthalene (Component of 91-20-3 0.00007 08 0.00061
POMT
Selenium Compounds SEC 0 08 0.000024
Toluene 108-88-3 0.00037 08 0.0034
40

u� �1®-r _rr__1
COPY of RECORD Date i : - /1 / 1 : :1
As entered i
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 2017
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 2017:' 0
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) %Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-18 CD-Coal—CC One ba filter 4.7:1 air to cloth ratio
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 W)
(in 0.1 feet)
P—Coal—CC VERTICAL STACK 1 30 1 2 75 18.56 3500 1 One Ba filter
42

Operating Scenario: OS—33 Emission Source/Group ID:ES—Coal—CC
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2017)
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%2017 2017 2017 2017
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
2017
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)
2017
CO CO 08 `0
NOx NOx 08 0
TSP TSP 08 0
PM10 PM10 08 0
PM2.5. PM2.5 08 0
S02 S02 08 0
VOC VOC 08 0
HAP/TAP Emissions Emission
CAS Estimation Control Emission
Pollutants (in ( ) HAP/TAPS Method Code Efficiency. Factor EF Control
see instructions
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2017
43

Submitted:COPY of RECORD Date l I
enteredin 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 2017
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) [213
.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: 30500311Brick Manufacture—Curing Firing ; Curing and Firing: Gas—fired
Tunnel Kilns
5. Throughput/units in 2017: 0
(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)
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)
ERP for ES—K3K,
EP—K3 VERTICAL STACK 35 4.92 99.95 33.79 38544.24 ES—K3D1 AND
ES—K3D2
44

Operating Scenario: OS— 10 Emission Source/Group ID: ES—K3K
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2017)
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:
Jan—Feb +Dec o arch—May o une—Aug. o Sept.—Nova o
2017 25/0 2017 25/0 2017 25/0 2017 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
2017
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)
2017
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
Estimation Emission
Pollutants (In (see instructions) HAP/TAPS Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2017
45

_ /� I �
DIG No—r 0oRri�
COPY of RECORD Date Submitted: 11 1 1 :2 :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 2017
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 MACT] AOS—Coal/Natural
3. Operating Scenario ID/Description: OS —25/10/Natural gas/propane/coal—fired kiln#3
4. SCC Numb er/Description: 305003 11/Brick Manufacture—Curing Firing ; Curing and Firing: Gas—fired
Tunnel Kilns
5. Throughput/units in 2017: 0
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) % Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-15 CD—K3DLA Dry limestone adsorber
9.Emission Release Point(EPP) 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)
P—K3DLA VERTICAL STACK 75.1 4.92 470.03 43.6 49734.5 dry limestone
absorber
-� 46

Operating Scenario: OS—25 Emission Source/Group ID: ES—K3K
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2017)
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% f017
e—Aug. 25% Sept.—Nov. 25%
2 2017 2017
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
2017
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)
2017
CO CO 08 0
NOx NOx 08 0
TSP TSP 08 0
PM10 PM10 08. 0
PM2.5 PM2.5 08 0
S02 S02 08 0
VOC VOC. 08 0
HAP/TAP Emissions Emission Control
CAS HAP/TAPS Estimation Emission
Pollutants (In
(see instructions) ffi
Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) structions (Net after all controls)
See In
2017
47

enteredCOPY of RECORD Date Submitted: 6/18/2018 16:24:17
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 2017
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) [213
.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: 30500311Brick Manufacture—Curing Firing ; Curing and Firing: Gas—fired
Tunnel Kilns
5. Throughput/units in 2017: L4.44-54 TON/yr vQv �
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) % Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
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/sec) Rate(Acfm)
Rectangle(L x W)
(in 0.1 feet)
P—K41)LA VERTICAL STACK 75.13 4.92 469 43.64 49780.13 Dry limestone
adsorber on Kiln 4.
48

Operating Scenario: OS—21 Emission Source/Group ID: ES—K4K
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2017)
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 25% arch—May 25% une—Aug. 25% ISept.—Nov. 25%
2017 2017 2017 2017
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
2017
Emission
Criteria . Emissions-- Estimation Control
Pollutant Criteria Method Efficienc Emission
(NAAant Code Pollutants. Code (Net ate y Factor Ef Control
Pollutants
(Tons/Year) (See all controls)
Instructions
2017
CO CO 59.95 08 0
NOx NOx 25.28 08 0
TSP TSP 50.1 f 08 0
PM10 PM10 50.11 08 0
PM2.5 PM2.5 50.11 08 0-
S02 S02 0.83 t 08 0
VOC. VOC 1.73 08 0
Emission
-- Emissions Estimation Control
HAP/TAP CAS Emission
HAP/TAPS Method Efficiency EF Control
Pollutants (In Alphabetical Order) (see instructions) Code (Net after all Factor
(Pounds/Year)
(See controls)
Instructions
2017 .
Arsenic Unlisted Compounds( ASC—Other 4.47807 08 0 0.000031 AFTER
Specify.Component of ASC
Benzene 71-43-2 .418.9166 08 0 0.0029 AFTER
Cadmium Metal(elemental 7440-43-9 . 2.16681 08 0 0.000015 AFTER
unreacted,Com onent of CDC
Chlorine• 7782-50-5 187.7902 08 0 0.0013 AFTER
Chromic acid (VI) (Component of So1CR6 CRC 7738=94-5 7.36715 08 0 0.000051 AFTER
!ED
h lhex 1 hthalate EHP 117-81-7 . 288.908 08 0 0.002 AFTER
chlorobenzene , 1,4— 106-46-7 6.93379 08 0 0.000048 AFTER
49

Ethyl chloride chloroethane 75-00-3, 82.33878 08 0 0.00057 AFTER
Fluorides (sum of all fluoride 'L3�`� • ©���
compounds 16984-48-8 43 2 08 0 Q9t 23
Formaldehyde 50-00-0 23.9 08 0
Hydrogen chloride (hydrochloric 4�,f qm7
acid) 7647-01-0 C 08 0 0.03 AFTER
Hydrogen fluoride(hydrofluoric 144q•9
acid as mass of HF-Component of 7664-39-3 --866-.72#- 08 90 006 AFTER
Fluorides) 0.01
Lead Unlisted Compounds(Specify PBC—Other 21.6681 08 0 0.00015 AFTER
and Component of PBC
Mercury,vapor(Component of 7439-97-6 1.08341 08 0 0.0000075 AFTER
HGC
Methyl chloride 74-87-3 96.78418 08 0 0.00067 AFTER
Methyl iodide 74-88-4 13.43422 08 0 0.000093 AFTER
Naphthalene(Component of 91-20-3 9.38951 08 0 0.000065
POMT
Nickel metal(Component of NIC 7440-02-0 10.40069 08 0 0.000072 AFTER
Selenium Compounds SEC 33.22442 08 0 0.00023 AFTER
Styrene 100-42-5 2.88908 08 0 0.00002 AFTER
Toluene 108-88-3 23.11264 08 0 0:00016 AFTER
Fro'n aw re V-eec- /-ZO Y/'-6 9 4-Oy I /Z;X n 4- '0 -.1711
r..Jr��� Ci/s�/ !J`J /V• \ //, i Y�//r ya wV z 0,®s
50

COPY f.RECORD Date Submitted:, 11 / :1
seer i ' 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 2017
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
y 4. SCC Number/Description: 30500397/Brick Manufacture; *Other Not Classified
5. Throughput/units in 2017: 0
(e.g.production or fuel use):
6. Fuel Information. (If fuel is used) %Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional 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.
)
in 0.1 feet)
P—RUMBLE VERTICAL STACK 44.95 1.312 72.05 40.02 3246.27 Rumbler Ba house
51

Operating Scenario: OS—36 Emission Source/Group ID:
ES—RUMBLE
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2017)
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% V0In7
—Aug. 25% Sept.—Nov. 25%
2 2017 2017
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
2017
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAA Code Pollutants Method Code (Net afterFactor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2017
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
Pollutants (In HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2017
52

COPY of RECORD Date Submitted: 1 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 2017
1. Emission Source ID (from permit) or IS-14.15A
Emission Source Group ID
2. Emission Source Description: propane vaporizer(1.3 million Btu per hour per burner)
3. Operating Scenario ID/Description: OS— 19/Propane Vaporizer
4. SCC Number/Description: 3 05003 97/Brick Manufacture ; *Other Not Classified
5. Throughput/units in 2017: 0
(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#): (F) (Feet/sec) (Acfm)
Rectangle(L x W)
(in 0.1 feet)
FEI—FG FUGITIVE(NO 1 72 TArea= 1 ERP for Fugitive
STACK sources
53

Operating Scenario: OS— 19 Emission Source/Group ID: IS-14.15A
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2017)
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%
2017 2017 ?2017 2017
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
2017
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Ef eiency Emission
(NAA Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2017
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP CAS Emissions Emission Control
Pollutants (In HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2017
54

Facility Total CY 2017 Emissions Summary
COPY of RECORD Date Submitted: /16/ 1 :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 2017
Record Facility-Wide Totals From all Permitted and Non-Permitted Air Pollutant Emission Sources
Green House Gases Pollutants(GHG)
Actual Emissions Tons/Year
Pollutant CAS 2017 2016 % Change
Criteria Pollutants
Actual Emissions Tons/Year
Pollutant CAS 2017 2016 % Change
CO CO 82.34 67.68 21.660751%
NOx NOx 32.37 26.61 21.64599%
PM TSP TSP 66.62 54.1 23.142338%
PM 10 PM 10 64.32 52.85 21.702936%
PM2.5 PM2.5 64.32 52.83 21.749%
SO2 SO2 0.83 .68 22.05882%
VOC VOC 4.57 3.88 17.783506%
Hazardous Air Pollutants HAPS and/or Toxic Air Pollutants TAPs
Actual Emissions (Pounds/Year)
Pollutant I CAS 1 2017 1 2016 % Change
Pollutant Group:Arsenic Compounds(total mass of elemental AS, arsine and all inorganic compounds) Group
Sum:4.47807
- _ Arsenic Unlisted Compounds (Specify ASC-Other 4.47807 3.68048 21.670809%
Component of ASC
Pollutant Grou :Cadmium compounds total mass inc elemental metal Group Sum:2.16681
Cadmium Metal(elemental unreacted, 7440-43-9 2.16681 1.78088 21.670752%
Component of CDC
Pollutant Grou :Chromium VI Soluble Chromate Compounds(Component of CRC Group Sum:7.36715
Chromic acid(VI)(Component of So1CR6 CRC 7738-94-5 7.36715 6.05498 T
21.670925%
Pollutant Grou :Chromium-All/Total Inc Chromium VI categories,metal and Others GroupSum:7.36715
Chromic acid (VI) (Component of 7738-94-5 7.36715 6.05498 21.670925%
- So1CR6 CRC
E
Pollutant Grou :Lead and Lead compounds Group Sum:21.66816
Lead Unlisted Compounds(Specify PBC-Other 21.66816 17.80888 21.670536%
55

and Component of PBC
Pollutant Grou :Mercu Compounds-all total mass,inc Ha Vapor Group Sum:1.08341
Mercury,vapor Com onent of HGC 7439-97-6 1.08341 .89044 j 21.671314%
Pollutant Grou :Nickel Com ounds,.sum.total mass,inc elemental Group Sum_ :10.40069
Nickel metal (Component.of NIC. 7440-02-0 10.40069 8.5482 21.671118%
Pollutant Grou zPol c clic Or anic Matter(Specific Compounds from OA PS for TV Group Sum:9.38958
Naphthalene(Component of POMTV 91-20-3 9.38958 7.71728 21.66955%
Benzene 71-43-2 418.91684 344.30304 21.670967%
Chlorine 7782-5075 187.7902 154.3425 21.671093%
Di 2-eth lhex 1 hthalate DEHP 117-81-7 288.908 237.45 21.671085%
Dichlorobenzene , 1,4- 106-46-7 6.93393 5.69911 21.66689%
Ethyl chloride chloroethane 75-00-3 82.33878 67.67325 21.671097%
Fluorides(sum of all fluoride 16984-48-8 1333.3104 1899.6 -29.81099%
compounds
Formaldehyde 50-00-0 23.90827 19.61912 21.862095%
Hexane,n= 1-10-54-3 0.19853 .459 -56.747272%
Hydrogen chloride(hydrochloric acid 7647-01-0 4333.62 3561.75 21.671093%
Hydrogen fluoride(hydrofluoric acid
as mass of HF-Component of 7664-39-3 866.724 1187.25 -26.997347%
Fluorides
Methyl chloride 74-87-3 96.78418 79.54575 21.671083%
Methyl iodide 74-88-4 13.43422 11.04143 21.671013%
Selenium Compounds SEC 33.22442 27.30676 21.671036%
Styrene 100-42-5 2.88908 2.3745 21.67109%
Toluene 108-88-3 23.11301 18.99687 21.667467%
56

COPY EC to Submitted: 11 l201 16:2 : 7
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
Comments From Facility:
57

SECTION 2
2017 SUPPORTING EMISSION CALCULATIONS
General Shale Brick, Inc. Moncure, NC Facility I CY 2017 Emissions Inventory
Trinity Consultants

Title: 2017 Air Emission Inventory
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID 1900009
Critical Parameters Table
Parameter-- ' Value
ape eft F
Actual Brick Production 0 tons per year
Actual Sawdust Usage 0 tpy
A-J�?""'c4m bustio�so -eg-D ekhove*�KiIL,3,,,,AiAAo§ot1qt 4"_ ,y- _ - e py t
Actual Brick Production(Natural Gas) 0 tPy
Actual Brick Production(Coal&NG) 0 tPy
Actual Gas Usage 0 scf/yr
Actual Coal Usage 0 tPy
mb' tidnS6�nrce�--!Rrick-h ;-MM 4 ndAssoei r e)rs
-0 us aven
Actual Brick Production(Natural Gas) 144,454 tpy
Actual Brick Production(Coal&NG) 0 tpy
Actual Brick Production(Coal&NG) 0 lb/hr
Acutal Gas Usage 318.020388 scf/yr
Actual Coal U sage 0 tPy
"Waste—Wood t6i Cape F6f,:,
Number of Cyclones I
Sawdust preparation 0 hr/yr
Cla
Actual Raw Material Processed 201400 tpy
Hours of operations 2,024 hr/yr
lyl
'Ritc Canoe or
Process Throughput 144.454 tpy
Simdj).y.yer-Cape Feakzu
Hours of operations 450 hr/yr
t
Actual Brick Production 144,454 t
Py
Baghouse Efficiency 99.8%
Hours of operation-Brick Haven 3,500 hr/yr
Hours of operations-Cape Fear 0 hr/yr
„ ,„Vacuum
Hours of operations-Cape Fear(VS I) 0 hr/yr
Hours of operations-Brick Haven(VS2) 1.500 hr/yr
Hours of operations-Brick Haven,(VS3)-Kiln 3 1000 hr/yr
Hetifsefeperatiens Bfie1E4laN,efl(V84&VS5 0 hf�yf
V,FI 1-11i T 4'$Qr 0 Flyash silo Throughput 0 tPy
'7z
Cement silo Throughput 0 tpy
Mixer LoadinE Throughput 0 tpy
-ggfe ate" 0 g a
Aggregate Loading Throughput 0 tPy
Hours of operations 0 br/yr
Usage
Diesel Tank 64,044 gal/yr
Gasoline Tank 5,788 gal/yr
Waste Oil Tank 693 gal/yr
Motor Oil Tank 51 gal/yr
Brick Oil Tank 7,675 gal/yr
Gear Oil Tank 404 gall
Reference:
Information Provided by Warren Paschal,General Shale Brick,Inc.,June 11,2018
Support Calculations File: General Shale Moncure CY2017 EI.xlsx
Printed:6/18/2018 Page 1 of 35 Sheet: Input

Title: 2017 Air Emission Inventory
Source ID#: ES-KI,ES-K2,ES-SDI
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID# 1900009
Brick Processing System-Cape Fear
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.
Pa'r`afileter Value
Actual Brick Production- 0 tpy
Actual Sawdust Usage
EMISSION CALCULATIONS
Emissions are calculated by the following equation:
I
Yearly Emissions
Emission Factor(lb/tons brick) Brick Production(tpy)=Emissions(lb/yr)
Emissions(lb/yr)12000 lb/ton=Emissions(tpy)
Note: The Formaldehyde emissions are multiplied by the wood usage instead of bricks usage.
•� Support Calculations File:General Shale Moncure CY2017 El.xlsx
Printed:6/18/2018 Page 2 of 35 Sheet Bdck-CF(G-66)

Source: ES-K1,ES-K2,ES-SD1 Sawdust Kilns 1&2 and sawdust dryer
Actual Annual Process Throughput: - Tons/yr
Brick Kiln Fuel: Wood
"Annual` Annual'
Emission IHactora(IbJtori
TAP NO CAS NO Emission Rate Emission Rate
_ Fred bricks produced)
Pollutant °` (lbs/yr) ",- (TPY).:,. Fl
_
PM 0.675 d 0 0.00
PM-10 0.675 ' ° 0 0.00
PM 2.5 0.675 ° 0 0.00
SO2 e 0 0.00
NOx 0.37 'd 0 0.00
VOC 0.18 0 0.00
CO' 0.344 d 0 0.00
1,4-dichlorobenzene 36 I06-46-7 0.00E+00 0.00E+00
2-butanone(MEK) 70 78-93-3 2.20E-04 'b 0.00E+00 0.00E+00
2-methylphenol(cresol) 35 95-48-7 2.40E-09 ab 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 0.00E+00 0.00E+00
Arsenic 9 ARSENICCPDS 2.10E-05 0.00E+00 0.00E+00
Benzene 12 71-43-2 5.60E-04 'b 0.00E+00 0.00E+00
Beryllium 16 BERYLCPDS 3.10E-07 °° 0.00E+00 0.00E+00
Bis(2-ethylhexyl)phthalate;di(2-
ethylhexyl)phthalate 39 117-87-7 1.40E-04 'b 0.00E+00 0.00E+00
Bromomethane(Methyl Bromide) HAP 74-83-9 4.40E-05 a6 0.00E+00 0.00E+00
Cadmium 23 CADMIUMCPDS 2.20E-05 aa0.00E+00 0.00E+00
Carbon Disulfide 27 75-15-0 1.80E-05 ab 0.00E+00 0.00E+00
Carbon tetrachloride 28 56-23-5 3.80E-07 ab 0.00E+00 0.00E+00
Chlorine 29 0.00E+00 0.00E+00
Chloroethane(Ethyl Choroethane) HAP 75-00-3 0.00E+00 0.00E+00
Chloroform 31 67-66-3 3.80E-07 'b 0.00E+00 0.00E+00
Chloromethane(Methlyl Chloride) HAP 74-87-3 0.0014 'b 0.00E+00 O.00E+00
Chromium(expressed as chromic
acid) HAP CROMCPDS 4.80E-05 0.00E+00 0.00E+00
Cobalt HAP 7440-48-4 0.00E+00 0.00E+00
Diethylphthalate HAP 84-66-2 0.00E+00 0.00E+00
Dimethylphthalate HAP 131-11-3 2.40E-09 'b 0.00E+00 0.00E+00
Di-n-butylphthalate HAP 84-74-2 1.60E-05 'b 0.00E+00 0.00E+00
Ethylbenzene HAP 100-41-4 1.00E-05 a6 0.00E+00 0.00E+00
Fluorine 50 0.00E+00 0.00E+00
Formaldehyde 51 50-00-0 6.63E-03 c 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 0.17 at 0.00E+00
Hydrogen Sulfide 60 7783-06-4 0.00E+00 0.00E+00
lodomethane(Methyl Iodide) HAP 74-88-4 -2.40E-04 'b O.00E+00 0.00E+00
Lead HAP LEADCPDS 1.20E-04 ' 0.00E+00 0.00E+00
M-/p-Xylene HAP 108-38-3/106-42-3 2.90E-05 "b 0.00E+00 0.00E+00
Manganese 62 MANGCPDS 4.80E-04 ' 0.00E+00 0.00E+00
1]1-Trichloroethane
(methylchloroform) 68 71-55-6 5.20E-07 'b 0.00E+00 0.00E+00
Methylene Chloride 69 74-87-3 6.20E-05 a6 0.00E+00 O.00E+00
Mercury 66 MERCCPDS 1.10E-05 0.00E+00 O.00E+00
Naphthalene HAP 91-20-3 2.40E-09 a6 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 a6 0.00E+00 0.00E+00
Ozone 0.00E+00 0.00E+00
Perch]oroethylene
(Tetrachloroethene) 81 •127-18-4 3.80E-07 °b 0.00E+00 0.00E+00
Phenol 82 108-95-2 1.00E-04 a6 0.00E+00 0.00E+00
Phosphine 71 0.00E+00 0.00E+00
Support Calculations File:General Shale Moncure CY2017 Elxlsx
Printed:6/182018 Page 3 of 35 Sheet:Brick-CF(G-66)

Phosphorus HAP 7723-14-0 5.50E-04 °' 0.00E+00 0.00E+00
Selenium HAP SEC 4.70E-05 0.00E+00 0.00E+00
Styrene 91 100-42-5 4.20E-06 °n 0.00E+00 0.00E+00
Toluene 97 108-88-3 4.30E-04 °n 0.00E+00 0.00E+00
Total Fluorides(including HF) 50 16984-48-8 0.27 n 0.00 0.00E+00
Trichlomfluoromethane 100 75-69-4 1.00E-06 " 0.00E+00 0.00E+00
Vinyl acetate HAP 108-05-4 1.90E-07 ab 0.00E+00 0.00E+00
Xylene 104 1330-20-7 3.63E-05 I 0.00E+00 0.00E+00
°Emission factors from AP-42,Section 11.3,8/97
as Table 11.3-7 for sawdust fired kilns and sawdust dryer.
°n Table 11.3-6 for sawdust fired kilns and sawdust dryer.
Table 11.3-2 for sawdust fired kiln and sawdust dryer.
ad Table 11.3-3 for sawdust fired kilns.
a` Table 11.3-5 for sawdust fired kilns and sawdust dryer.
°r Table 11.3-4 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= tpy
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
,H1gliest Emtsslons��Rate '"Emission-"
Pollutant. ''Tested(Ib/hr): 'Factor(Ib/ton)
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 Run Emissions Emission
Pollutant Rate Tested(lb/hr)' Factor(tb/ton)
SO2 0.56 0.029
S02 factor for wood combustion AP42-Section 1.6 0.025 lb/MMBtu
IvNBtu for wood=Tons wood fired *2000 lb/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= - Ibslyr '
r
Support Calculations File:General Shale Moncure CY2017 FJ_xlsx
Printed:6/18/2018 - Page 4 of 35 Sheet:Brick-CF(G-66)

I �
Title: 2017 Air Emission Inventory
Source ID#: ESWK
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
Brick Processing System-Brick Haven-Kiln 3
Source: ES-K3K Kiln 3
Actual Brick Production: 0 Tons/yr
Coal Fired 0 Tons/yr -
Brick Kiln Fuel: Coal/NG
60%Coal
40%Natural Gas
Control Eff.of HF 90% (NESHAP Requirement)
Une�ontrolle_l Unconkrolled
);mtsston i' 7A< Emisston
TAP NO ' Factor for ` Ref Factor for Nested Total
Coalfrom A Natural Gas ; Emtsston 6t Annual ,Annual `_,,
tEoll (Iblfon Ib/ton Y` E mIbts/s irp ns Emtorsns/�o`rn lb/ton s
PM 4.12E-01 g 0.00 0:00E+00
PM-10 2.03E-01 g 0.00 0.00E+00
PM-2.5 2:03E-01 g 0.00 0.00E+00
S02 38.000 IF2.86E-02 d 0.00 0.00E+00
NOx 8.13E-01 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 al 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
HCl 57 5.82E-02 d 0.000 0.00E+00
I I I Ji-ichloroethane 68 1.70E-05 ac 4.70E-06 of 0.00E+00 0.00E+00
(methylchloroform)
Methylene Chloride 69 8.00E-07 ae 0.00E+00 0.00E+00
Perchloroethylene 81 2.80E-06 of 0.00E+00 0.00E+00
(Tetrachloroethene)
1,1-dichloroethane HAP 5.00E-06 ae 0.00E+00 0.00E+00
1,4-dichlorobenzene 36 3.20E-06 ac 4:80E-05 of 0.00E+00 0.00E+00
2-butanone(MEK). 70 2.50E-04 ae 2.20E-04 of 0.00E+00 0.00E+00
2-Hexanone NA 9.40E-07 ac 8.50E-05 of 0.00E+00 0.00E+00
2-methylphenol(cresol) 35 2.20E-06 de O: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 all 0.00E+00 0.00E+00
Acetone NA 6.80E-04 ac 1.70E-03 of O.00E+00 0.00E+00
Arsenic 9 1.30E-04 ag 3.10E-05 ab 0.00E+00 0.00E+00
Benzene 12 2.90E-04 ae 2.90E-03 ac 0:00E+00 O:00E+00
Benzoic Acid 2.50E-04 ae 0.00E+-00 0.00E+00
Beryllium 16 1.60E-05 ag 4.20E-07 ah O:00E+00 O.00E+00
Bis(2=ethylhexyl)phthalate;di(2- 39 7.30E-OS ac 200E-03 of 0.00E+00 0.00E+00
! ethylhexyl)phthalate
Bromomethane(Methyl 0.00E+00 0.00E+00
Bromide) HAP 2.40E-OS
Butylbenzylphthalate NA 1.20E-06 ac 1.80E-05 of 0.00E+00 0.00E+00
Cadmium 23 1.50E-05 ah 0.00E+00 0.00E+00
Support Calculations - File: General Shale Moncure CY2017 El.xlsx
Printed:6/18/2018 Page 5 of 35 - Sheet: Brick-BH(ES-K3K_G12)NG&Coal

Carbon Disulfide 27 2.30E-06 ae 4.30E-05 of 0.00E+00 0.00E+00
Carbon tetrachloride 28 1.00E-07 ae 0.00E+00 0.00E+00
Chlorobenzene HAP 2.10E-05 ae 0.00E+00 0.00E+00
Chloroethane(Ethyl HAP 1.10E-05 5.70E-04 0.00E+00 0.00E+00
Choroethane)
Chloroform 31 1.00E-07 ae 0.00E+00 0.00E+00
Chloromethane(Methyl HAP 1.10E-04 ae 6.70E-04 of 0.00E+00 0.00E+00
Chloride)
Soluble Chromate Compounds 5.10E-05 ab 0.00E+00 0.00E+00
Cobalt 2.10E-06 ah 0.00E+00 0.00E+00
Dibenzofuran NA 3.60E-07 ae 0.00E+00 0.00E+00
Diethylphthalate HAP 1.40E-06 ae 2.40E-04 of 0.00E+00 0.00E+00
Dimethylphthalate HAP 7.80E-07 - 0.00E+00 O.00E+00
Di-n-butylphthalate HAP 1.40E-04 of 0.00E+00 0.00E+00
Di-n-octylphthalate 1.20E-05 - 0.00E+00 0.00E+00
Ethylbenzene HAP 2.10E-05 - 4.40E-05 of 0.00E+00 0.00E+00
Formaldehyde 51 7.50E-02 b 0.00E+00 0.00E+00
Iodomethane(Methyl Iodide) HAP 9.30E-05 of 0.00E+00 0.00E+00
Isophorone. HAP 3.00E-05 - 0.00E+00 0.00E+00
Lead NA 1.50E-04 ah 0.00E+00 0.00E+00
M-/p-Xylene HAP 1.30E-04 - 6.70E-05 of 0.00E+00 0.00E+00
Manganese 62 2.90E-04 ag 2.90E-04 ah 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 - 6.50E-05 - 0.00E+00 0.00E+00
Nickel 75 7.20E-05 ah O:00E+00 O.00E+00
o-Xylene HAP 4.70E-05 - 5.80E-05 - 0.00E+00 0.00E+00
Perchloroethylene of 0.00E+00 0.00E+00
(Tetrachloroethene) 81 2.80E-06
Phenol 82 3.50E-05 ae 8.60E-05 ae 0.00E+00 0.00E+00
Phosphorus HAP 9.80E-04 ag 0.00E+00 0.00E+00
Selenium NA 2.30E-04 ab 0.00E+00 0.00E+00
Styrene 91 1.00E-07 - 2.00E-05 de 0.00E+00 0.00E+00
Toluene 97 2.50E-04 - 1.60E-04 ac 0.00E+00 0.00E+00
Total Fluorides 50 6.10E-01 c 0.00E+00 0.00E+00
Trichl orofluorom ethane 100 1.40E-05 de 0.00E+00 0.00E+00
Vinyl acetate HAP 1.00E-07 ae 0.00E+00 0.00E+00
'Emission factors from AP-42,Section 11.3,8/97
as Table 1 1.3-1 for uncontrolled coal-fired and natural gas-fired kilns.
PM for condensible PM= 0.59 lb/ton
ab Table 11.3-3 for coal-fired and natural gas-fired kilns.
ae Table 11.3-4 for coal-fired and natural gas-fired kilns
ad Table 1 1.3-5 for brick kilns.
a`Table 11.3-6 for coal-fired kilns.
arTable 11.3-6 for natural gas-fired kilns
'Table 11.3-7 for coal-fired kilns.
ah Table 11.3-7 for natural gas-fired kilns.
a'Factor is from AP-42 Background Document testing at
Marseilles Brick which has the same type of kiln
a3 Soluble Chromate Compounds is the regulated NC TAP
b Emission factors from AP-42,Section 1.4,7/98. The emissions factor in in Ib/mmft 3 of gas. The actual gas rate:
`- Formaldehyde Emission Factor=
0.0 MMBtu/hr/1020 Btu/ft3* 1 Oh Btu/MMBtu/10^(ft3/MMft3)= 0.0000 mmft3/hr
` Using AP-42 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*(I -CE)
dTesting 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 CY2017 El,xlsx
Printed:6/18/2018 Page 6 of 35 Sheet: Brick-BH(ES-K3K_G12)NG&Coal

Highest Run,-
Emissions Rate Emtss'ionnFactor
Pollutant Tested,(Ib/he) (lblton)
HF* 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
**SOZ data was from a September 27,2004 engineering test on Kiln 3 with
a 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=
NOx Emission Factor= 9.67 lb/hr / 11.89 ton/hr
NOx Emission Factor= 0.813 lb/ton
f AP-42 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
s 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 lbs of brick/hr
Emission Factors are as follows:
- verage:
Emissions Rate Emission`'Factor
Pollutant - Vested(lb/hr)
PM 6.1 0.412
PM10 3 0.203
PM2.1 3 0.203
Support Calculations File: General Shale Moncure CY2017 EI.xlsx
Printed:6/18/2018 Page 7 of 35 Sheet:_Brick-BH(ES-K3K_G12)NG&Coal

I f
Title: 2017 Air Emission Inventory
Source ID#: ES-K3D1,ES-K3D2,ES-K3D3
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
g
Source: ES43D1,ES-K3D2,ES-K3D3 Brick Dryers 1,2,and 3 on Kiln 3
Actual Production - Tons/yr
- Brick Dryer Fuel: NG/Propane
Aririval I
k Em>tssion Factors : Emission Rate Em>tss>ton 5,.
Pollutant (16%ton fired br>Icks produced) (lb/yr) "Rate(TP:lolx
PM 0.187 ac 0.00' 0.00
PM-10 0.187 a° 0.00 0.00
PM-2.5 0.187 ac 0.00 ' 0.00
SO2 0.00
NOx 0.098 as 0.00 0.00
VOC 6.03 ab 0.06 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:
Support Calculations File: General Shale Moncure CY2017 EI.xlsx
Printed:6/18/2018 Page 8 of 36 Sheet: Brick-BH(ES-K3K G12)(total)

Title: 2017 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
Actual Brick Production: 144,454 Tons/yr
Coal Fired 0 Tons/yr
Brick Kiln Fuel: Coal/NG
Percentages if Coal Fired: 60%Coal
40%Natural Gas
Control Eft.of HF 90% (NESHAP Requirement)
1N CY 2017 Fired NO Only
Uncontrolled" -
_ a'Emission
TAP`NO Factor-for - Tested ''•
, �'Natural Gas" F° Emission- Annual,, `.=TotaLAnnaaGr
Pollutant from AP42 Ref Faeiors`" Ref` Emissions r. =Emissions
(Ib/ton) (lb/ton), -` (Ib/yr) '�,.(ton/yr)
PM 1.04E-01 e,as 100,229 50.11
PM-10 1.04E-01 e,aa 100,229 50.11
PM-2.5 1.04E-01 e,as 100,229 50.11
S02 2.86E-02 d 1,653 0.83
NOx 3.50E-01 A 50,559 25.28
VOC 2.40E-02 ad 3,467 1.73
CO 0.83 ai 119,897 59.95
Chlorine 29 1.30E-03 of 188 0.094
HF 59 5.77E-03 e 833.4 4.17E-01
HCl 57 2.63E-02 e 3,797 1.90E+00
lll-Trichloroethane 68 4.70E-06 of 6.79E-01 3.39E-04
(methylchloroform).
Methylene Chloride 69 0.00E+00 0.00E+00
Perchloroethylene 81 2.80E-06 of 4.04E-01 2.02E-04
(Tetrachloroethene)
1,1-dichloroethane HAP 0.00E+00 0.00E+00
1,4-dichlorobenzene 36 4.80E-05 of 6.93E+00 3.47E-03
2-butanone(MEK) 70 2.20E-04 of 3.18E+01 1.59E-02
2-Hexanone NA 8.50E-05 of 1.23E+01 6.14E-03
2-methylphenol(cresol) 35 0.00E+00 0.00E+00
-- 2-methylnaphthalene NA 5.70E-05 of 8.23E+00 4.12E-03
Antimony NA 2.70E-05 A 3.90E+00 1.95E-03
Acetone NA 1.70E-03 of 2.46E+02 1.23E-01
Arsenic 9 3.10E-05 A 4.48E+00 2.24E-03
Benzene 12 2.90E-03 4.19E+02 2.09E-01
Benzoic Acid 0.00E+00 0.00E+00
Beryllium 16 4.20E-07 A 6.07E-02 3.03E-05
Support Calculations File:General Shale Moncure CY2017 El.xlsx
Printed:6/18/2018 Page 9 of 35 Sheet: Brick-BH(ES-K4K_G12)NG&Coal

Bis(2-ethylhexyl)phthalate; 39 2.00E-03 °r 2.89E+02 1.44E-01
di(2-ethylhexyl)phthalate
Bromomethane(Methyl HAP 0.00E+00 O.00E+00
Bromide)
Support Calculations File: General Shale Moncure CY2017 El.xlsx
Printed:6/18/2018 Page 10 of 35 Sheet: Brick-BH(ES-K4K_G12)NG&Coal

Butylbenzylphthal ate NA ' 1.80E-05 ar 2.60E+00 1.30E-03
Cadmium 23 1.50E-05 ah 2.17E+00 1.08E-03
Carbon Disulfide 27 430E-05 ar 6.21E+00 3.11E-03
Carbon tetrachloride 28 0.00E+00 0.00E+00
Chlorobenzene HAP 0.00E+00 0.00E+00.
Chloroethane(Ethyl HAP 5.70E-04 ar 8.23E+01 4.12E-02
Chloride)
Chloroform 31 0.00E+00 0.00E+00
Chloromethane(Methyl HAP 6.70E-04 at 9.68E+01 4.84E-02
Chloride)
Soluble Chromate 5.10E-05 ah 7.37E+00 3.68E-03
Compounds
Cobalt 2.10E-06 ah 3.03E-01 1.52E-04
Dibenzofuran NA 0.00E+00 0.00E+00
Diethylphthalate HAP 2.40E-04 ar 3.47E+01 1.73E-02
Dimethylphthalate HAP 0.00E+00 0.00E+00
Di-n-butylphthalate HAP 1.40E-04 If 2.02E+01 1.01E-02
Di-n-octylphthalate 0.00E+60 0.00E+00
Ethylbenzene HAP 4.40E-05 If 6.36E+00 3.18E-03
Formaldehyde 51 7.50E-02 b 2.339E+01 1.19E-02
Iodomethane(Methyl HAP 9.30E-05 If 1.34E+01 6.72E-03
Iodide)
Isophorone HAP 0.00E+00 0.00E+00
Lead NA 1.50E-04 ah 2.17E+01 1.08E-02
M-/p-Xylene HAP 6.70E-05 ar 9.68E+00 4.84E-03
Manganese 62 2.90E-04 ah 4.19E+01 2.09E-02
Mercury 66 7.50E-06 nh 1.08E+00 5.42E-04
Naphthalene HAP 6.50E-05 ae 9.39E+00 4.69E-03
Nickel 75 7.20E-05 ah 1.04E+01 5.20E-03
o-Xylene HAP 5.80E-05 ae 8.38E+00 4.19E-03
Perchloroethylene ar 4.04E-01 2.02E-04
(Tetrachloroethene) 81 2.80E-06
Phenol 82 8.60E-05 ae 1.24E+01 6.21E-03
Phosphorus HAP 0.00E+00 0.00E+00
Selenium NA 2.30E-04 ah 3.32E+01 1.66E-02
Styrene 91 2.00E-05 ae 2.89E+00 1.44E-03
Toluene 97 1.60E-04 ae 2.31E+01 1.16E-02
Total Fluorides 50 923E-03 0 1,333 6.67E-01
Trichlorofluoromethane 100 0.00E+00 0.00E+00
Vinyl acetate HAP 0.00E+00 0.00E+00
'Emission factors from AP-42,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 11.3-4 for coal-fired and natural gas-fired kilns
'J Table 11.3-5 for brick kilns.
'rTable 11.3-6 for natural gas-fired kilns
ATable 11.3-7 for natural gas-fired kilns. -
°'Factor is from AP-42 Background Document testing at
Marseilles Brick which has the same type of kiln
Soluble Chromate Compounds is the regulated NC TAP
b Emission factors from AP-42,Section 1.4,7/98. The emissions factor in in Ib/mmft3 of gas. The actual gas rate:
Actual Gas Usage= 318,020,388 scf/yr = 318.02 mmft3/yr
Support Calculations File:.General Shale Moncure CY2017 Ei.xlsx
Printed:6/18/2018 Page 11 of 35 Sheet: Brick-BH(ES-K4K_G12)NG&Coal

Using AP-42 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
d Testing was performed on Kiln 4 on February 10,2006. Emissions Factors are as follows:
Process weight rate during test 19.93 ton/hr
tg est un
:,Emfssions'Rate EMissionFactor
Pollutant`:' ^ . Tested(Ib/hr) (Ib)ton)
HF* 7.6 0.381
HCl* 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
**SCh 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:
verage
"Emissions Rate EmissioldY actor
Pollutant." Tested(Ib/hr)"
PM 1.6 0.10
HCl 0.41 2.628E-02
HF 0.09 5.769E-03
Support Calculations File: General Shale Moncure CY2017 El.xlsx
Printed:6/18/2018 Page 12 of 35 Sheet: Brick-BH(ES-MK_G12)NG 8 Coal

_I
Title: 2017 Air Emission,Inventory
Source.ID#: ES-K4D1,ES-K4132,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
Actual Production: 144,454 Tons/yr
Brick Dryer Fuel: NG/Propane
� Annual �4Annual
M
Emission Factor-(lb/ton Aeed inis'sion Rate Emission s'
Pollutant t* br>Icksrproduced) (lb/yr) Rate(TPY)
PM 0.187 ad 27,013 13.51
PM-10 0.187 ad 27,013 13.51
PM-2.5 0.187 ad 27,013 13.51
SO2 .
NOx 0.098 as 14,156 7.08
VOC 0.03 ab 4,334 ' 2.17
CO 0.31 ac 44,781 22.39
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 1 l.3-5 for brick dryer.
ac Table 11.3-5 for brick dryer.
ad Table 11.3-1 for brick dryer.
b The formaldehyde emissions from the dryer are included in the kiln calculation.
Support Calculations File: General Shale Moncure CY2017 Ei.xlsx
Printed:6/18/2018 Page 13 of 35 Sheet: Brick-BH(ES-K4K_G12)(total)

Title: 2017 Air Emission Inventory
Source ID#: `ES-K1,ES-K2,ES-SDI,ES-K2K,ES-K4K,ES-K4D1,ES-K4D2,ES-K4D3
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
'k •'`• ` "' - `; '_; 'Cape Fear• Brick Haven.` Actual Emissions.
� .
Wood Kilhs&
C(3Number' TAP/HAP 'Dryora3&2_ 1Cdn3K(a Kiln3Dryer Bric7haven3 Kiln4K,In Kiln4 Briokhaven4 .Total.
Pollutant,- - (tpY)s (tpy) (lb/yr)` Total(ton%yr) -:(Ipy) Dryer(tpy).Total(tons/yr) Total(Ib/yr) `. TPY
PM 0.00E+00 0.00E+00 0.00E+00 5.01E+01 1.35E+01 63.62 1.27E+45 63.62
PM-10 0.00E+00 0.00E+00 0.00E+40 5.01E+01 1.35E+01 63.62 1.27E+05 63.62
PM 2.5 0.00E+00 0.00E+00 O.00E+00 5.01E+01 1.35E+01 63.62 1:27E+05 63.62
S02 O.UOE+00 0.00E+00 O.00E+00 8.26E-01 0.00E+00 0.83 1.65E+03 U.83
NOs 0.00E+00 0.00E+00 0.00E+00 2.53E+01 7.08E+00 32.36 6.47E+04 32.36
VOC 0.00E+00 0.00E+00 0.00E+00 1.73E+00 2.17E+00 3.90 7.80E+03 3.90
CO 0.00E+00 0.00E+00 0.00E+00 5.99E+01 2.24E+01 82.34 1.65E+05 92.34
Pounds/yr, -
,WoodKilns& -
•. 'Dryers 1&Z; Kdn 3 Kiln Kiln'3 Dryer Brickhaven 3 Kiln 4.Kdn Kiln 4 Brickhaven 4 Total
ti ,_ - - ;(Ibfyr).. _,�(Ib%yr)• n �16/Yr�:<;. Total:(Ib/yr) ,(Iblyr) Dryer(Ib/yr)�-Total(16/y, Total(Iblyr)< -- -TPY
1,4-dichlorobcnzene 36 106-46-7 0.00E+00 O.00E+0O 0.00E+00 6.93E+00 6.93E+00 6.93E+00 3.47E-03
2-butanone(MEK) 70 78-93-3 0.00E+00 0.00E+00 0.00E+00 3.18E+0I 3.18E+0I 3.18E+0I 1.59E-02
2-methylphenol(cresol) 35 95-49-7 0.00E+00 0.00E+00 0.00E+00 O:00E+00 0.00E+00 0.00E+00 0.00E+00
Acryloniirile 4 107-13-1 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00
Antimony HAP ANTIMONYCPDS 0.00E+00 0.00E+00 0.00E+00 3.90E+00 3.90E+00 3.90E+00 1.95E-03
Arsenic 9 ARSENICCPDS 0.00E+00 0.00E+00 0.00E+00 4.48E+00 448E+00 4.48E+00 2.24E-03
Benzene 12 71-43-2 0.00E+00 0.00E+00 0.00E+00 4.19E+02 419E+02 4.19E+02 2.09E-01
Beryllium IG BERYLCPDS 0.00E+00 0.00E+00 0.00E+00 6.07E-02 6.07E-02 6.07E-02 3.03E-05
Bis(2-cthylhcsyl)phthalalc;di(2- .00E+00 117-87-7 0 "
cthylhcxyl)phthalatc 39 0.00E+00 0.00E+00 2.89E+02 2.89E+02 2.89E+02 1.44E-01
Bromomethane(Methyl Bromide) HAP 74-83-9 0.00E+00 O:00E+00 O:00E+00 O.00E+00 0.00E+00 0.00E+00 0.00E+00
Cadmium 23 CADMIUMCPDS 0.00E+00 0.00E+00 0.00E+00 2.17E+0U 2.17E+00 2.17E+00 1.08E-03
Carbon Disulfide 27 75-15-0 0.00E+00 0.00E+00 0.00E+00 6.21E+00 6.21E+00 6.21E+00 3.11E-03
Carbon tetrachloride 28 56-23-5 0.00E+00 0.00E+00 0.00E+00 0.00E+00 O.00E+00 0.00E+00 0.00E+00
Chlorine 29 0.00E+00 0.00E+00 0.00E+40 1.88E+02 1.88E+02 1.88E+02 9.39E-02
Chloroethanc(Ethyl Chorcethanc) HAP - 75-00-3 0.00E+00 0.00E+00 0.00E+00 8.23E+01 8.23E+01 8.23E+OI 4.12E-02
Chloroform 31 67-66-3 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00
Chloromethane(Methly Chloride) HAP 74-87-3 0.00E+00 0.00E+00 0.00E+00 9.68E+01 9.68E+01 9.68E+01 4.84E.02
Chromium(expressed as chromic acid) HAP CROMCPDS 0.00E+00 0.00E+00 0.00E+00 7.37E+00 7.37E+00 7.37E+00 3.68E-03
Cobalt HAP 7440-48-4 0.00E+00 0.00E+00 0.00E+00 3.03E-01 3.03E-01 3.03E-01 1.52E-04
Diethylphlhalate HAP 84-66-2 0.00E+00 0.00E+00 0.00E+00 3.47E+01 3.47E+01 3.47E+01 1.73E-02
Dimethylphthalate - HAP 131-I I-3 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 O.00E+00
Di-n-butvlpllthalale HAP 84-74-2 0.00E+00 O.00E+00 I 0.00E+00 2.02E+01 2.02E+0I 2.02E+01 1.01E-02
Ethvlbcnzcnc HAP 100-41-4 0.00E+00 0.00E+00 0.00E+00 6.36E+00 6.36E+00 6.36E+00 3.18E-03
Fluorine 50 O.UOE+00 0.00E+00 - 0.00E+00 0.00E+00 0.00E+00 200E+00 0.00E+00
Formaldehyde 51 50-00-0 0.00E+00 0.00E+00 0.00E+00 2.39E+01 2.39E+0I 2.39E+01 1.19E-02
Hydrazinc HAP 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00
.HF 59 76(A-39-3 0.00E+00 0.00E+00 0.00E+00 8.33E+02 8.33E+02 8.33E+02 4.17E-01
HCI 57 7647-01-0 0.00E+00 0.00E+00 0.00E+00 3.80E+03 3.80E+03 3.80E+03 1.90E+00
Hydrogen Sulfide 60 7783-064 0.00E+00 0.00E+00 0.00E+00 .0.00E+00 0.00E+00 0.00E+00 0.00E+00
lodomethane(Mclhyl Iodide) HAP 74-88-4 0.00E+00 0.00E+00 0.00E+00 1.34E+01 1.34E+01 1.34E+01 6.72E-03
Lead HAP LEADCPDS 0.00E+00 0.00E+00 0.00E+00 2.17E+OI 2.17E+01 2.17E+01 1.08E-02
M-/p-Xylcnc HAP 108-38-3/106-42-3 0.00E+00 0.00E+00 2110E+00 - 9.68E+00 9.68E+00 9.68E+00 4.84E-03
Manganese - 62 MANGCPDS 0.00E+00 0.00E+00 0.00E+00 4.19E+0I 4.19E+01 4.19E+01 2.09E-02
III-Trichlorcethanc 68 71-55-6 0.00E+00
(methylehlorofoml) 0.00E+00 0.00E+00 6.79E-01 6.79E-01 6.79E-01 3.39E-04
Methylene Chloride 69 74-87-3 0.00E+00 O.00E+00 200E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00
Mercury 66 MERCCPDS 0.00E+00 0.00E+00 0.00E+00 1.08E+00 1.08E+00 1.08E+00 5.42E-04
Naphthalene. HAP 91-20-3 0.00E+00 200E+00 0.00E+00 9.39E+00 939E+00 9.39E+00 4.69E-03
Nickel 75 NICKCPDS 0.00E+00 0.00E+00 0.00E+00 1.04E+01 1.04E+01 1.04E+01 5.20E-03
o-Xylcnc HAP 95-47-6 0.00E+00 O.00E+00 0.00E+00 8.38E+00 -8.38E+00 -8.38E+00 4.19E-03
Ozone 0.00E+00 O.UOE+00 200E+00 O:00E+00 0.00E+00 0.00E+00 0.00E+00
Perchloroethviene(Tetrachloroethene) 81 127-18-4 0.00E+00 0.00E+00 0.00E+00 4.04E-01 4.04E-01 4.04E-01 2.02E-04
Phenol 82 109-95-2 0.00E+00 O.00E+00 0.00E+00 1.24E+01 1.24E+01 1.24E+01 6.21E-03
Phosphine 71 0.00E+00 O:00E+00 0.00E+00 0.00E+00 0.00E+00 O.00E+00 0.00E+00
Phosphorus HAP 7723-14-0 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 O.00E+00 0.00E+00
Selenium HAP SEC 0.00E+00 O.00E+00 0.00E+00 3.32E+01 3.32E+01 3.32E+01 I.66E-02
St- 91 10042-5 0.00E+00 0.00E+00 0.00E+00 2.89E+00 2.89E+00 2.89E+00 1.44E-03
Toluene 97 108-88-3 0.00E+00 O.00E+00 0.00E+00 2.31E+01 2.31E+OI 2.31E+01 1 1.16E-02
Total Fluorides(including HF) 50 16984-48-8 0.00E+00 0.00E+00 0.00E+00 1.33E+03 1.33E+03 1.33E+03 6.67E-01
Trichloro0uoromelhanc 100 75-694 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00
Viral acetate HAP I08-05-4 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 U.00E+00
Xylcnc 104 1330-20-7 0.00E+00. 0.00E+00 0.00E+00 1.%IE+0l 1.81E+01 1:81E+0I 9.03E-03
Support Calculations File:General Shale Moncure CY2017 EI.xlsx
Printed:611 812 01 8 Page 14 of 35 Sheet MckSum

Title: 2017 Air Emission Inventory
Source ID#: ES-Coal-CC
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
Coal Crusher
Source: ES-Coal-CC Coal Crusher
Controls: CD-Coal-CC NA
Efficiency: 99.0%
Maximum Production: 0 tpy Did Not Operate in 2017
Uncontrolled h Annual
Emission
Emission Factor Emission
Pollutant lb/ton Rate(lb%yr)
( ) Rate(.TYVY
PM 1.10 0.00E+00 0.00E+00
PM-10 1.10 0.00E+00 O.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
` 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.
Uncontrolled Factor= 0.11 lb/ton
(1-.90)
1.1 lb/ton
A
Support Calculations File: General Shale Moncure CY2017 El.xlsx
Printed:6/18/2018 Page 15 of 35 Sheet: ES-Coal Crusher

i
Title: 2017 Air Emission Inventory
Source ID#: ES-WFS
{ Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
{ Wood Fucl/Sawdust System
2017 AEI Numbers
j
Source: ES-WFS Wood Fuel/Sawdust System
Hours'of Operation 0 hrs
Wood Fuel/Sawdust System
Control: CD-SD-DC1 Dust Collector
y
Description: Two conveyors,which feed materials to the two screens,are both controlled by a dust collector._
t
EPN: EP-SD-DC1 Did Not Operate in 2017
Source: ES-SD-SC1 M Screen
ES-SD=SC2 M Screen
ES-SD-CV1 Transfer Screw Conveyor
{ ES-SD-CV2 Screen Feed Screw Conveyor
Variables: Hours of Operation
7
Factors:
Exit Concentration= 0.01 gr/dscf
Flow Rate for System= 2100 cfm
Bagfilter Efficiency- 99%
Emissions Before Control
PM Emissions=Emissions After Control/(1 -.Efficiency)
PM Emissions= 180 lb/hr
Emissions After Control
PM Emissions=Exit Concentration* 1 lb/,7,000 gr*Flow Rate*60 min/hr
EM Emissions_ 0 180'` lb/hr .
0 "lb/:,c
1
V
Support Calculations . File: General Shale Moncure CY2017 El.xlsx
Printed:6/18/2018 Page 16 of 35 Sheet: Controlled New WFS(G-21)

, I
Wood Fuel/Sawdust System
Controls: CD-SD-DC2 Dust Collector(2300 elm)
Description: Dust collector is used for the PM exhaust from the hammermill and cyclone.
EPN:" EP-SD-DC2
Did Not Operate in 2017
Source: ES-SD-CYC Cyclone
ES-SD-HM Hammermill
Variables: Hours of Operation
Factors:
Exit Concentration= 0.01 gr/dscf
Flow Rate for System= 2345 cfm
Bagfilter Efficiency= 99%
Emissions Before Control
PM Emissions=Emissions After Control/(1 -Efficiency)
PM Emissions= 20.1 lb/hr
Emissions After Control
I
PM Emissions=Exit Concentration* 1 lb/7,000 gr*Flow Rate*60 min/hr
rPM.Emissions X0.201` e 1b/l777-
_f
Support Calculations File: General Shale Moncure CY2017 EI.xlsx
Printed:6/18/2018 Page 17 of 35 Sheet: Controlled New WFS(G-21)

f
a �
Wood Fuel/Sawdust System
Controls: CD-SD-BVl Bin Vent Filter
Description: Storage silo,which is connected to a bin vent filter,is used as storage for the product.
EPN: EP-SD-BV1
Did Not Operate in 2017
Source: ES-SD-SDS Sawdust Silo
Variables: Hours of Operation
Factors:
Exit Concentration= 0.01 gr/dscf
Flow Rate for System= 400 cfm
Bagfilter Efficiency= 99%
i
Emissions Before Control
PM Emissions=Emissions After Control/(1 -Efficiency)
PM Emissions= 3.4 lb/hr
Emissions After Control
PM Emissions=Exit Concentration* 1 lb/7,000 gr*Flow Rate*60 min/hr
PiVi Emissions`= 0.034 lb/hr
0 0 lb/yr
i
Support Calculations File: General Shale Moncure CY2017 El.xlsx
Printed:6/1 812 0 1 8 Page 18 of 35 Sheet: Controlled New WFS(G-21)

; r
Wood Fuel/Sawdust System
Controls: CD-SD-BV2 Bin Vent Filter
C
Description:
Product from the screen is sent to the surge hopper,which is equipped with a bin vent filter.
EPN: EP-SD=BV2
- Did Not Operate in 2017
Source: ES-SD-SH Surge Hopper
Factors:
Exit Concentration= 0.01 gr/dscf
Flow Rate for System= 400 cfm
Bagf]ter Efficiency= 99%
Emissions Before Control
PM Emissions=Emissions After Control/(I -Efficiency) .
PM Emissions= 3.4 lb/hr
Emissions After Control
PM Emissions=Exit Concentration* I lb/7,000 gr*Flow Rate*60 min/hr
PM•Emissions 0 034. ]b%hr
0 0 N' ili%yr
Total WFS Emissions
'i WFS -•Total
Pollutant (Controlle'd) 'TPY+,
PM 0.00E+00 0.00E+00
PM-10 0.00E+00 0.00E+00
PM-2.5 0.00E+00 0.00E+00
k
Support Calculations File: General Shale Moncure CY2017 ElAu
Printed:6/18/2018 Page 19 of 35 Sheet: Controlled New WFS(G-21)

rl
;
Title: 2017 Air Emission Inventory
E Source ID#: Clay Handling
( Facility: General Shale Brick,Inc.
Location: S4oncure,NC
Facility ID#: 1900009,
Source: ES-CH Clay Handling Equipment
Description: This scenario represents the crushing/grinding/screening/storage operations as they
are currently operating.
EPN: Fugitive
Controls: NA
i Factors for Grinding&Screening:
l 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
i Actual Raw Material Processed 202,400 tpy
Maximum Hours of Operation 2,024 hrs/yr
Control Efficiency for PM 0 % No Control Devices
ID Descrrptjon,'
F-PC Primary crusher(clay handling
equipment 200 tph)
F-SS1 &F-SS2 Two scalping screens(clay
handling equipment 200 tph)
NSPS
F-HM Hammermill#1 (clay handling
equipment 200 tph)
F-FS1 -F-FS9 One-bank of nine finishing screens
(clay handling equipment 200 tph)
F-FC4 Finishing Conveyor#4(clay
handling equipment 200 tph)
t NSPS
F-FC5 Finishing Conveyor#5(clay
handling equipment 200 tph)
NSPS
Pollutant Actual;Emssions _-,a
Name" on r
PM - 5,060.00 2.53
PM-10 466 0.23
PM-2.5 466 0.23
I ,
Support Calculations File: General Shale Moncure CY2017 EI.xlsx
Printed:6/18/2018 Page 20 of 35 Sheet: Clay Handling(G-71)

itr
I
Title: 2017 Air Emission Inventory
Source ID#: Clay Handling
I Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
Source: ES-CH Clay Handling Equipment
SAMPLE CALCULATIONS
Grindint?&Screening Emissions
PM Actual Emissions(lbs/yr)
0.025 lb/ton *202400 tpy = 5060.00 lbs/yr
I
PM Actual Emissions(tons/yr)
5060 Ibs/yr/2000lb/ton = 2.53 tpy
PM-10 Actual Emissions(lbs/hr)
0.0023 lb/ton *202400 tpy = 465.520 lbs/yr
PM-10 Actual Emissions(tons/yr)
465.52 lbs/yr/2000lb/ton = 0.23 tpy
PM-2.5 Actual Emissions(lbs/hr)
0.0023 lb/ton *202400 tpy = 465.520 Ibs/yr
PM-2.5 Actual Emissions(tons/yr)
465.52 lbs/yr/2000lb/ton = 0.23 tpy
Support Calculations File: General Shale Moncure CY2017 EI.xlsx
Printed:6/18/2018 Page 21 of 35 Sheet: Clay Handling(G-71)

2017 Air Emiss 2017 Air Emission Inventory General Shale Brick Inc.
Source: Intersite Conveyor Moncure Plant
Source:. Conveyor from Cape Fear Plant to
Brickhaven Plant F-C-CFBH
I
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
where:E=emission factor(lb/ton)
k=particle size multiplier(dimensionless)
U=mean wind speed(mph)
M=material moisture content(%)
E=k(0.0032)[(U/5)^1.3/(M/2)^l.4]lb/ton
where:
k= 0.74 for PM<=30 microns;
0.35 for PM<=10 microns;
0.053 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
PM<=10 microns:
0.35* 0.0032* [(15 mpW5)^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 Throughput ' Drops .;
ID Description
t
From,Cape Fear to ES-C Conveyor 144,454
Brickhaven 1
Pollutant Potential Emissions(per}emission source)
Name'. (Ibs/yr) `(ton's/yr)
PM 149.90 0.07
PM-10 70.90 0.04
PM-2.5 10.74 0.01
Emissions based on Drop Equations Equations @ 200 tph,which is the process weight rate for Brickhaven's
existing Grinding Room.
Support Calculations File: General Shale Moncure CY2017 El.xlsx
Printed:6/18/2018 Page 22 of 35 Sheet: Intersiteconv(Clay Handling)

SAMPLE CALCULATIONS
Grindinti&Sereenine Emissions
PM Potential Emissions(lbs/yr)
0.001 lb/ton* 144454 tpy* 1 drop= 149.90 lbs/hr
PM Potential Emissions(tons/yr)
150 /20001b/ton = 0.07 tons/yr
TOTAL EMISSION CALCULATIONS FOR CLAY HANDLING
Pollutant Potential-Emissions(per emssioit"source),'.; u.- ;
Name" Jlbs/yr) , ',(tons/30
PM 5209.90 2.60
PM10 536.42 0.27
PM2.5 476.26 0.24
Support Calculations File: General Shale Moncure CY2017 El.xlsx
Printed:6/18/2018 Page 23 of 35 Sheet: IntersiteConv(Clay Handling)

Title: 2017 Air Emission Inventory
Source ID#: ES-CR-5,ES-CR-6,and ES-CR-7
Description: Texturing Operations
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID #: 1900009
Texturing Operations
Sand Blasting Cabinets
Parameter Value
Actual Brick Production-CF 0:tons/yr
Actual Brick Production-BH 144,454 tons/yr _
Hrs of Operation-Brick Haven 3500 hr/yr
Hrs of Operation-Cape Fear 0 hr/yr
Baghouse Efficiency 99.8%
Approach: AP-42 Section 11.3,Table 11.3-2
AP-42 Emission Factor for PM/PM-10/PM-2.5 0.0036 lbs/ton brick
Basis: Actual Brick Production Rate-Cape Fear 0 tpy
Actual Brick Production Rate-Brickhaven 144454 tpy
Scale Up Factor Potentials 1
Two Texturing Operations
Controlled by CD-CR6BF, CD-CR7BF, CD-CR7BF2 and CD-CR7BF3
EMISSION CALCULATIONS
Brick Haven Brick Haven Cape Fear Total
Pollutant ` ,Actual,Emissions,' Actual Emissions,, Actual Emissions•.
Name ' bs/y r " . tons/ r lbs/ r :tons/ r' lbs7. r tons% r
PM 520.03 0.260 0.00 0.000 520.03 0.260
PM-10 520.03 0.260 0.00 0.000 520.03 0.260
PM-2.5 1 520.03 0.260 1 0.00 0.000 520.03 0.260
Support Calculations File: General Shale Moncure CY2017 EI.xlsx
Printed:6/18/2018 Page 24 of 35 Sheet: Text(G-69)

Title: 2017 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
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
Gas Usage(Calculated 1.10294E-01 mmft3/yr
based upon hours of operation)_
i
ncontro e, , m►ssion Factor Emissions , Emissions
Pollutant (lb/mmft3) Ref Rate(lb/yr) Rate(toy)
PM 0.52 3 3.11 E+00 1.55E-03
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 ' 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 132E-09
3-Methylchloranthrene 1.80E-06 ' 1.99E-07 9.93E-II
7,12-Dimethylbenz(a)anathracene 1.60E-05 ' 1.76E-06 8.82E-10
Acenaphthene 1.80E-06 ' 1.99E-07 9.93E-II
Acenaphtylene 1.80E-06 ' 1.99E-07 9.93E-II
Acetaldehyde 1.52E-05 z 1.68E-06 838E-10
Acrolein 1.80E-05 2 1.99E-06 9.93E-10
Anthracene 2.40E-06 ' 2.65E-07 132E-10
Ammonia 3.20E+00 2 3.53E-01 1.76E-04
Benz(a)anthracene 1.80E-06 ' 1.99E-07 9.93E-II
Benzene 2.10E-03- 232E-04 1.16E-07
Support Calculations File: General Shale Moncure CY2017 EI.xlsx
Printed:6/18/2018 Page 25 of 35 Sheet: Dryer(ES-CD-8)

Benzo(a)pyrene 1.20E-06 ' 1.32E-07' 6.62E-I I
j Benzo(b)fluoranthene 1.80E-06 1 1.99E-07 9.93E-11
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-I'1
Butane 2.1 1 232E-0T 1.16E-04
Chrysene 1.80E-06 ' 1.99E-07 9.93E-II
Dibenzo(a,h)anthracene 1.20E-06 t 132E-07 6.62E-II
Dichlorobenzene. 1.20E-03 ' 1.3)2E-04 6.62E-08
Ethane 3.1 I 3.42E-01 1.71 E-04
Fluoranthen_e. 3.00E-06 I 3.31E-07 1.65E-10
Fluorene 2.80E-06 3.09E-07 1.54E-10
Formaldehyde 7.50E-02 .8.27E-03 4.14E-06
J Hexane 1.8 ' 1.99E-01 9.93E-05
Indeno(1,2,3-cd)pyrene 1.80E-06 ' 1.99E-07 9.93E-11
Naphthalene 6.10E-04 ' 6.73E-05 3.36E-08
Pentane 2.6 I 2'.87E-01 1.43E-04
Phenanathrene 1.70E-05 1.88E-06 938E-10
Propane 1.6 1.76E-01 .8.82E-05
Pyrene 5.00E-06 5.57E-07 2.76E-10
Toluene 3.40E-03 ' 3.75E-04 1.88E-07
Arsenic 0.00E+00 , 2 0.00E+001 O.00E+00
Barium 4.40E-03 ' 4.85E-04 2.43E-07
Beryllium. 0.00E+00 z 0.00E+00 0.00E+00
Cadmium O.00E+00 2 0.00E+00 0.00E+00
Chromium(as chromic acid) O.00E+00 2 0.00E+00 6.00E+00
Cobalt . 8.40E-05 ' 9.26E-06 4.63E-09
Copper 8.50E-04 ' 938E-05 4.69E-08
CO2 1.20E+05 2 132E+04 6.62E+00
Lead 5.00E-04 ' 5.51 E-05 2.76E-08
Manganese O.00E+00 2 O.00E+00 . 0.00E+00
Mercury 0.00E+00 2 0.00E+00 0.00E+00
Methane 230E+00 ' 2.54E-01 1.27E-04
Molybdenum 1.10E-03 ' 1.21E-04 6.07E-08
N20 2.20E+00 ' 2.43E-01 1.21E-04
Nickel 0.00E+00 z 0.00E+00 0.00E+00
- Selenium 2.40E-05 ' 2.65E-06 1.32E-09
Vanadium. 2.30E-03 ' 2.54E-04 1.27E-07
Zinc 2.90E-02 ' .3.20E-03 1..60E-06
I AP-42;Compilation of Air Pollutant Emission Factors Vol. 1-Stationary Sources USEPA,
5th ed.Section 1.4,3/98-Small Boilers-Uncontrolled
2 NC Department of Air Quality,Natural Gas Spreadsheets-Small Boiler-Uncontrolled
4
3 PM&PM-10 Emissions were calculated by adding natural gas combustion factors and(NC Spreadsheets
5 P for PM,PM-10 from NEI)and factors for industrial sand dryers(AP-42,Section 11.19)
Support Calculations file: General Shale Moncure CY2017 El.xlsx
Printed:.6/18/2018 Page 26 of 35 Sheet: Dryer(ES-CD-8)

I
,Parameter,.�<; Value
Maximum Hourly Coatings Rate 3.45 ton/hr
Actual Annual Coatings Rate 1,552.50 ton/yr
Industrial an ryer Emission
Factor* 2.00 lb/ton
PM/PM-10/PM-2.5 Emissions= 3.45 ton/hr*2 lb/ton
PM/PM-10/PM-2.5 Emissions= 6.90 lb/hr.
PM/PM-10/PM-2.5 Emissions= 1552.5 ton/yr*2 lb/ton
PM/PM-10/PM-2.5 Emissions= 3,105 lb/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
i 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.
r
Support Calculations File: General Shale Moncure CY2017 EI.xlsx
Printed:6/18/2018 Page 27 of 35 Sheet: Dryer(ES-CD-8)

Title: 2017 Air Emission Inventory
Source ID#:ES-VSI,-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 cfin
Bagfilter Efficiency= 99.9%
G-70 Hours of Operation-Cape Fear= - hr/yr
(IES-VS 1)
Hours of Operation-Brick Haven= 1,500 br/yr
(IES-VS2)
Total 1,500 hr/yr
G-22 Hours of Operation-Brick Haven= 2,000 hr/yr
(IES-VS3)-Kiln 3 Hi-Vac
Hours of Operation-Brick Haven= - hr/yr
(IES-VS4&-VS5)
Total 2,000 hr/yr
Emissions Before Control
PM Emissions=Emissions After Control/(1 -Efficiency)
PM Emissions= 120.0 Ib/hr
-Emissions After Control
PM Emissions=Exit Concentration* 1 lb/7;000 gr*Flow Rate*60 min/hr*(1-Efficiency)
PM Emissions= 0.120 lb/hr
PM-1"0 Emissions= 0.120 lb/hr
PM-2.5 Emissions= 0.120 lb/hr
EMISSION CALCULATIONS
Actual Emissions=PM Emissions,lb/hr(After Control)*Hours of Operation,,hr/yr
G-70(IES-VSI&-VS2)
Pollutant ",:: >1 Actual'"•Emissions-$I3 ° ',;' `, ;A'ctuaLEmissions=CF.- , :Total-Actual'Emissions
Name Ibs/ r tons/ r s (Ibs/yr) X01f$4r) `•, `-,:(Ibs/yr);.' (tons/yr)'-
PM 180.00 0.090 0.00 0.000 180.00 0.090
PM40 180.00 0.090 0.00 0.000 180.00 0.090
PM-2.5 180.00'. 0.090 0.00, 0.000 180.00 0.090'
- G-22'(IES-VS3,-VS4&-VS5)
Pollutant : .•Act6al:Emission's-VS3°' Actaal`Emissions-VS4-&VS5•.,jotalActuhlEmissions:
Name'.< Ibs/ r tons/ r _:';`(Ibs/yr) (tons/yr,) (Itis/Yr).:' .*`(tons/yr)
PM 240.00 0.120 0.00 0.000 240.00 0.120
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 CY2017 EI.xlsx
Printed:6/18/2018 Page 28 of 35 Sheet: Vacuums(G722&'G-70)

Title: 2017 Air Emission Inventory
Source ID ill: Storage Tanks
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID 4: 1900009
Note:Emissions carried over from CY2014.
K Tank Talk" Breathing o-rkj-
pg, Total.
E­ iisionsr
heighf, CapacityLosses In
"1017TAt! Losses' L
V,
N m -Turnovers
­Description/Contents, ,'. Size ",Numbers;
, u ' b T (lb/yr)" Oh/yr'Y""
Diesel 1,000 7 5 881 64,044 72.67
Gasoline 1,000 7 5 1,028 5,788 5.63
Waste Oil 275 5.25 3 225 693 3.08
Motor Oil 160 4.5 2.5 129 51 0.40
Brick Oil 350 _LL6." 3 291 7,675 L6-3 9
Gear Oil 350 1 6.55 1 3 346 404 LA17
Support Calculations File: General Shale Moncure CY2017 El.xlsx
Printed:6/18/2018 Page 29 of 35 Sheet: Storage Tanks(G-144)

Title: 2017 Air Emission Inventory
Source ID 0:ES-BP-FAS
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID M 1900009 Did Not Operate in 2017
•'Controlled Controlled Controlled
' Source. Em M ^PM10 pMrs
P ;
Control
„Emission Cin"ification "Emission .-Emission E,imssron
,Device:ID,
-'Source '.Code(SCC) -Factor' Factor 'F9ctin Throughput P1VFEmrssions`:V .' `PMioEmissions �`°PMj.5 missions "
Description r ;�;:' .(Ib%ton) (Ib/ton).. 6A'EINum ';'` `'(tpy)... (Ib/Y),=" `(tPY).': .(Ib/Y) (tPY) .':.(16fY)-°- "(tPY) yn
Flyash Sil 3-05-011-06 bin vent 0.0089 0.0049 0.0049 0 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00
a Controlled PM emission factors for aggregate transfer,pneumatic 0yash loading,pneumatic loading of cement silo,weigh hopper loading,and miser loading from AP42,Section
11.12-Concrete Balch Operations,(10/01).
- - ,Flyash
SiloFilling
Emissiod ''Flyash Silo Emissions"
--, Hazardous „
Air Factor:: Example Calculations:
'Pollutant (lb/ton) •' (Ib/y) (tpy)
Arsenic 1.00E-06 0.00E+00 0.00E+00 PM Potential Emissions(lbs/yr)
Beryllium 9.04E-08 O.00E+00 0.00E+00 0.009lb/ton•Olpy=lbs/yr 0lbs/yr
Cadmium 1.98E-08 0.00E+00 0.00E+00
Chromium 1.22E-06 0.00E+00 0.00E+00 PM Potential Emissions(tons/yr)
Lead 5.20E-07 O.00E+00 0.00E+00 0lbs/yr•'(I ton/2000lb)= 0.00E+00 tons/yr
Manganes 2.56E-07 0.00E+00 0.00E+00
Nickel 2.28E-06 0.00E+00 0.00E+00
Phosphoru 3.54E-06 0.00E+00 0.00E+00
Selenium 7.24E-08 0.00E+00 0.00E+00
Support Calculations File:General Shale Moncure CY2017 ElAs
Printed:611 812 01 8 Page 30 of 35 Sheet:Flyash Silo

Title: 2017 Air Emission Inventory
Source ID#:ES-BP-CS
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID M 1900009
Did Not Operate in 2017
Controlled Controlled
Source ,. '
Classi6catio Control PM. PMio >4
Emission:. Device IEmission Emission 2016AEI Throu h u , Emsn Code sSource r .Numbers isswis P(SCC) Fctor FaMo t .,PMEm FP .-
Descri tion.' -` -(lb/ton) ' (lb ton).,, .>(lli ton)-, J(Ibly) (tPY)> (IbIY) (Ib/Y) 1Cement Sil 3-05-011-07 bin vent 0.00099 0.00034 0.00034 0 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00
a Controlled PM emission factors for aggregate transfer,pneumatic flyash loading,pneumatic loading of cement silo,weigh hopper loading,and mixer loading from AP-42,
Section 11.12-Concrete Batch Operations,(10/01).
-"'Cement Silo
-Emission'-'CementSilo-Emissions'.
Hazardous Factors. 211
Air•` Example Calculations:
Pollutant -(lb/ton) (lb/y)" (fPY):.
Arsenic 4.24E-09 0.00E+00 0.00E+00 PM Potential Emissions(Ibs/yr)
Beryllium 4.86E-10 0.00E+00 0.00E+00 0.00099lb/ton"Olpy=Ibs/yr 0lbs/yr
Cadmium 4.86E-10 0.00E+00 0.00E+00
Chromium 2.90E-07 0.00E+00 0.00E+00 PM Potential Emissions(tons/yr)
Lead 1.09E-08 0.00E+00 0.00E+00 0lbs/yr•(1 ton/2000.lb)= 0.00E+00 tonslyr
Manganes 1.17E-07 0.00E+00 0.00E+00
Nickel 4.18E-05 0.00E+00 0.00E+00
Phosphona - -
Selenium - - -
1
Support Calculations File:General Shale Moncure CY2017 El.xlsx
Printed:6/1 812 01 8 Page 31 of 35 Sheet:Cement Silo

Title: 2017 Air Emission Inventory
Source ID Of: ES-BP-BM
Facility: General Shale Brick,Inc.
r Location: Moncure,NC
Facility ID H: 1900009
Did Not Operate in 2017
. , Controlled `controlled- `�
Source PM to
Control i
Classificahon .Device ID
Emission •Emission 2016AEI . 's
EmissionSourm Code(SCC),.". ' Factor' •Factor •'Numbers'„ :Throe Throughout, =PM�Emissions. = PMraEmissions .:.-PMx",Emissions:-,
' Descr tion :. . (lb/ton). ,. '_(lb/ton)' (lb/ton) ,..< `(tpy)_.' (Ib/Y) (tPY) (Ib/y)" (ipy) `'..IIb/Y) ``.;^''(1PY)- .'..
Mixer Loading 3-05-011-09 bagfilter 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 factors for aggregate transfer,pneumatic llpash loading,pneumatic loading of cement silo,weigh hopper loading,and mixer loading from AP-42,Section
+ 11.12-Concrete Batch Operations,(10101).
+Batch Mixer. '
Emission- Batch'Mixer Emissionsd
Hazardous Air, Factors - Example Calculations:
,Pollutant'. ,(lb/ton)".' (Ib/y) '(tPY)
Arsenic 1.87E-08 0.0000 0.00E+00 PM Potential Emissions(lbs/yr)
Beryllium - - - 0.01 llb/1on•0tpy=lbshr 0lbs/yr
Cadmium 7.10E-10 0.0000 0.00E+00
Chromium 1.27E-07 0.0000 0.00E+00 PM Potential Emissions(tonslyr)
Lead 3.66E-08 0.0000 0.00E+00 0Ibs/yr•(1 ton2000 lb) 0.00E+00 tonslyr
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 - - -
Support Calculations File:General Shale Moncure CY2017 ElAs
Printed:6/1812018 Page 32 o135 Sheet:Batch Mixer

EMISSION 2017 Air Emission Invento en 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 2017
Hours of Operation: 0 hrs
Factors:
Exit Concentration= 0.01 gr/dscf
Flow Rate for System= 5000 cfm
_ Bagfilter Efficiency= 95%
Emissions Before Control
PM/PM-1 0/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 Rate*60 min/hr
PM/PM-10/PM-2.5 Emissions= 0.429 lb/hr
0.00 lb/yr
0.00 tpy
Pollutant;, ^`, Controlled`Actual'Emissi Oils
,
Name (lbs/hr)4 ,'(lbs/yr) =(tons/yr)
PM 4.29E-01 0.00E+00 0.00E+00
PM-10 4.29E-01 O.00E+00 0:00E+00
PM-2.5 4.29E-01 0.00E+00 0.00E+00
Support Calculations File: General Shale Moncure CY2017 El.xlsx
Printed:6/18/2018 Page 33 of 35 Sheet Rumbler

Clay, .
Handling
- (.Including.
Coal Controlled ,'Intersite:. ': ...' Sand n Vacuum Cement Storage Total _To
SAS Number TAPMAP.. Brick, Grush�ng WFS. Conveyor) „Texturin It "er Systems FI ash Silo. Silo:`; $atch'Mixer Rumbler Tanks T)
Criteria Pollutants (tons/yr)
6.36E+01 0.00E+00 0.00E+00 2.60E+00 160E-01 1.55E-03 2.10E-01 0.00E+00 0.00E+00 0.00E+00 0.00E+00 1.33E+05 66.
6.36E+01 0.00E+00 0.00E+00 2.68E-01 2.60E-01 1.55E-03 2.10E-01 0.00E+00 0.00E+00 0.00E+00 0.00E+00 1.29E+05 64.
6.36E+01 0.00E+00 0.00E+00 2.38E-01 2.60E-01 1.55E-03 2.10E-01 0.00E+00 O.00E+00 0.00E+00 0.00E+00 1.29E+05 64.
8.26E-01 3.31E-05 1.65E+03 0.1
3.24E+01 5.51E-03 6.47E+04 32.
3.90E+00 3.03E-04 1.23E-01 I 8.05E+03 4.1
8.23E+01 4.63E-03 1.65E+05 82.
Hazardous Air Pollutants (lbs/yr)
106-46-7 36 6.93E+00 1.32E-04 6.93E+00 3.471
78-93-3 70 3.18E+01 3.18E+01 1.591
95-48-7 35 0.00E+00 0.00E+00 0.001
75-07-0 1.68E-06 .1.68E-06 8.381
107-02-8 1.99E-06 1.99E-06 9.931
107=13-1 4 0.00E+00 0.00E+00 0.001
7664-41-7 3.53E-01 3.53E-01 1.761
TIMONYCPDS HAP 3.90E+00 3.90E+00 1.951
RSENICCPDS 9 4.48E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 4.48E+00 2.241
71-43-2 12 4.19E+02 2.32E-04 4.19E+02 2.091
30-32-8 HAP 1.32E-07 1.32E-07 6.621
3ERYLCP.DS 16 6.07E-02 0.00E+00 0.00E+00 0.00E+00 - 6.07E-02 3.031
117-81-7 39 2.89E+02 2.89E+02 1.441
74-83-9 HAP 0.00E+00 0.00E+00 0.001
iDMIUMCPDS., 23 2.17E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 2.17E+00 1.081
75-15-0 27 6.21E+00 6.21E+00 3.111
56-23-5 28 0.00E+00 0.00E+00 0.00E
7782-50-5 29 1.88E+02 1.88E+02 0.(
75-00-3 HAP 8.23E+01 8.23E+01 4.121
67-66-3 31 0.00E+00 0.00E+00 0.00E
74-87-3 HAP 9.68E+01 9.68E+01 4.841
CROMCPDS HAP 7.37E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 7.37E+00 3.681
7440-48-4 HAP 3.03E-01 9.26E-06 3.03E-01 1.521
84-66-2 HAP 3.47E+01 3.47E+01 1.731
131-11-3 HAP 0.00E+00 0.00E+00 0.00E
84-74-2 HAP 2.02E+01 2.02E+01 1,011
100-41-4 HAP 6.36E+00 6.36E+00 3.181
7782-41-4 50 0.00E+00 0.00E+00 0.00E
50-00-0 51 2.39E+01 8.27E-03 2.39E+01 1.191
110-54-3 HAP 1.99E-01 1.99E-01 9.931

A5 Number , TAP/RAP, Brick Crushing r. WFS ,-. .Conyeyor)V: rTexturing' :'Dryer ;:;.Systems Flyash Silo $ilo': Batch Myer;• Rumbler Tanks (TIP
_. . _ r F.
LEADCPDS HAP 2.17E+01 5.51E-05 0.00E+00 0.00E+00 0.00E+00 2.17E+01 1.081
3-38-3/106-42-3 HAP 9.68E+00, 9.68E+00 4.841
VIANGCPDS 62 4.19E+01 0.00E+00 0.00E+00 0.00E+00 0.00E+00 4.19E+01 -2.091
71-55-6 71-55-6 6.79E-01 6.79E-01 3.391
75-09-2 74-87-3 0.00E+00 0.00E+00 0.00E
MERCCPDS MERCCPDS 1.08E+00 0.00E+00 1.08E+00 5.42I
91-20-3 HAP 9.39E+00 6.73E-05 9.39E+00 4.691
NICKCPDS 75 1.04E+01 0.00E+00 0.00E+00 0.00E+00 0.00E+00 1.04E+01 5.201
95-47-6 HAP 8.38E+00 8.38E+00 4.19I
0.00E+00 0.00E+00 0.001
127-18-4 81 4.04E-01 4.04E-01 2.021
108-95-2 82 1.242E+01 1.24E+01 6.211
7803-51-2 71 0.00E+00 0.00E+00 0.00E
7723-14-0 HAP 0.00E+00 0.00E+00 0.00E+00 0.00E+00 O.00E
SEC HAP 3.32E+01 2.65E-06 -O.00E+00 - - 3.32E+01 1.661
100-42-5 91 2.89E+00 2.89E+00 1.441
108-88-3 97 2.31E+01 3.75E-04 2.31E+01 1.161
16984-48-8 50 1.33E+03 1.33E+03 6.671
75-69-4 100 0.00E+00 0.00E+00 0.00E
108-05-4 HAP 0.00E+00 0.00E+00 0.00E
1330-20-7 104 1.81E+01 1.81E+01 9.031