AQ_F_1900009_20170627_EI_Cmb-EI-File

1 1
2016 Emissions Inventory Review / Data Tracking Form
Facility Name: General Shale Brick Inc. - Moncure Facility Facility ID: 1900009
Facility Assigned to: Data Entry: Chatham County
Classification: Stanley Williams Confidential Copy Submitted?
Title V 0 YES
No
Initial Review/Data Entry
0 Enter date received into ED. Date Received: 46, 27- ZO 17
Z Assigned to appropriate individual. Date Assigned: Date Due: /O< /S-2 61 7
❑ Paper copy submitted: One copy received with supporting documentation,certification form signed by responsible official,and
appears generally complete;OR
m Electronic copy submitted: Alf 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.
Er 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.
2 Evaluate"U"sources for significance and address according to policy.
0 Calculations/forms appear to add up correctly.
8 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.
Z Calculations and control efficiencies appear correct. Emission factors are the best available and most current factors appropriate
for the reporting facility(e.g. stack testing,AP-42,etc.).
® Review facility comments and address any issues.
❑ Update ED(Data Entry Main)if additional information is required(corrections due date and date received).
la Check all ED QA/QC reports.
Comparison with previous emission inventory must be made and outliers(> 10%)must be investigated and explained.
Z 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: 14) 5 2-0/7 Signature: 156.n(f,n �,..
Date Submitted to EI Coordinator: /0.5-ZO/7
Date Approved: 15I I Initials: w-I V

Facility Total CY 2016 Emission Summary.Recorded in ED Facility ID #: 1900009
Facility Name: General Shale Brick, Inc. 7Moncure Facility Permit#(s): 043844139
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 2016 CY 2015 Demini- %
from ED from Fees mus Change
CO CO 67.68 75.31 0.5 1-10.1%
NOx NOx 26.61 29.59 0.5 1 -10.1%
PM(TSP) TSP 54.10 60.72 0.5 1 -10.9%
PM10 PM10 52.85 58.85 0.5 1-10..2%
PM2.5 PM2.5 52.83 58.81 0.5 1-10.2%
S02 S02 0.680000 0.760000 0.5 -10.5%
VOC VOC 3.88 . 4.24 0.5 7 -8.5%
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPs) (Pounds/Year)
Pollutant CAS CY 2016 CY 2015 Demini- %
from ED from Fees mus Change
Antimony & Compounds(total mass, inc elemental SB) Not 3.57 10.0 'N/A
Reported
Antimony Unlisted Compounds- Specify Compoun< SBC-Other Not 3.57 10.0 N/A
(Component of SBC) Reported
Arsenic & Compounds(total mass of elemental AS, arsine and 3.68 4.10 0.01 I-10.2%
all inorganic compounds)
Arsenic Unlisted Compounds - Specify Compound ASC-Other 3.68 4.10 0.01 1-10.1%
(Component of ASC)
Beryllium & compounds(Total mass) Not 0.055490 1.0 N/A
Reported
Beryllium Metal (unreacted) (Component of BEC) 7440-41-7 Not 0.055490 1.0 N/A
Reported
10/05/2017 Page 1 of 4

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Facility Total CY 2016 Emission Summary Recorded in ED Facility ID #: 1900009
Facility Name: General Shale Brick Inc. -Moncure Facility Permit#(s): 04384T39
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPs) (Pounds/Year)
Pollutant CAS CY 2016 CY 2015 Demini- %
from ED from Fees mus Change
Cadmium & compounds(total mass includes elemental metal) 1.78 1.98 0.1 I-10.1%
Cadmium Metal, elemental, unreacted(Component( 7440-43-9 T:78----- -1:98-- -O-T 10:1016-- ---
CDC)
Chromium-AII/Total(includes Chromium (VI) categories, 6.05 6.74 0.1 1-10.2%
metal and others)
Chromic acid (VI) (Component of SolCR6 & CRC) 7738-94-5 6.05 6.74 0.011-10.1.%
Chromium (VI)Soluble Chromate Compounds (Component of 6.05 6.74 0.01 1-10.2%
CRC)
Chromic acid (VI) (Component of So1CR6 & CRC) 7738-94-5 6.05 6.74 0.01 1 -10.1%
Cobalt& compounds Not 0.277440 1.0 I N/A
Reported
Cobalt Unlisted Compounds - Specify Compound COC-Other Not 0.277440 1.0 N/A
(Component of COC) Reported
Lead& compounds 17.81 19.82 1.0 1-10.1%
Lead Unlisted Compounds- Specify Compound PBC-Other 17.81 19.82 10.0 -1.0.1.%
(Component of PBC)
Manganese & compounds Not 38.31 10.0 I N/A
Reported
Manganese Unlisted Compounds- Specify Compoui MNC-Other Not 38.31 10.0 N/A
(Component of MNC) Reported
Mercury & Compounds-all total mass includes Hg Vapor 0.890440 0.990860 0.001 1-10.1%
Mercury,vapor(Component of HGC) 7439-97-6 0.890440 0.990860 0.001 1 -10.1%
Nickel& Compounds, sum total mass includes elemental 8.55 9.51 1.0
Nickel metal (Component of NIC) 7440-02-0 8.55 9.51 1.0 -10..1%
Polycyclic Organic Matter(Specific Compounds from OAQPS 7.72 8.59 1.0 I-10.1
yo
for Tip
Naphthalene (Component of 83329/POMTV) 91-20-3 7.72 8.59 1.0 -10.1%
Benzene 71-43-2 344.30 383.13 1.0 1-10.1%
Carbon disulfide 75-15-0 Not 5.68 10.0 N/A
Reported
10/05/2017 Page 2 of 4

Facility Total CY 2016 Emission Summary Recordea n 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 2016 CY 2015 Demini- %
from ED from Fees mus Change
Chlorine 7782-50-5 154.34 171.75 100.0 -10.1%
DEHP(Di(2-ethylhexyl)phthalate) 117-81-7 237.45 264.23 10.0 1 -10.1%
Dibutylphthalate 84-74-2 Not 18.50 100.0 N/A
Reported
Dichlorobenzene(p), 1,4- 106-46-7 5.70 6.34 1.0 1-10.1%
Ethyl benzene 100-41-4 Not 5.81 100.0 N/A
Reported
Ethyl chloride (chloroethane) 75-00-3 67.67 75.30 10.0 -10.1.%
Fluorides (sum of all fluoride compounds as mass of 16984-48-8 1,899.60 8,060.00 10.0 P6.4%
ion)
Formaldehyde 50-00-0 19.62 18.46 10.0 6.3%
Hexane, n- 110-54-3 0.459000 0.165420 100.0 1177.5%
Hydrogen chloride (hydrochloric acid) 7647-01-0 3,561.75 3,474.60 100.0 2.5%
55.7%
Hydrogen fluoride (hydrofluoric acid as mass of HF) 7664-39-3 1,187.25 762.30 100.0
(Component of 16984488/Fluorides)
MEK(methyl ethyl ketone, 2-butanone) 78-93-3 Not 29.07 100.0r
Reported
Methyl chloride(chloromethane) 74-87-3 79.55 88.52 1.0 -10.1%
Methyl chlorof6rm 71-55-6 Not 0.620940 Mq N/A
Reported
Methyl iodide (iodomethane) 74-88-4 11.04 . 12.29 10.0T10.1%
Perchloroethylene (tetrachloroethylene) 127-18-4 Not 0.369920 1 Ofl N/A
Reported
Phenol 108-95-2 Not 11.36 100.0 N/A
Reported
Selenium Compounds SEC 27.31 30.39 10.0 -10.1%
Styrene 100-42-5 2.37 2.64 100.0 -10.1%
Toluene 108-88-3 19.00 21.14 100.0 1 -10.1%,
Vinyl acetate 108-05-4 Not 0.013210 100.0 N/A
Reported
10/05/2017 Page 3 of 4

Facility Total CY 2016 Emission Summary Recorded in ED Facility ID #: 1900009
Facility Name: General Shale Brick Inc. -Moncure Facility Permit#(s): 04384T39
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPs)- (Pounds/Year)
Pollutant CAS CY 2016 CY 2015 Demini-
from ED from Fees mus. Change
Xylene (mixed isomers) 1330-20-7 Not 16.51 100.0 N/A
Reported
Largest Individual HAP Hydrogen chloride (hydrochloric acid) 3,561.75 lbs
Total HAP Emissions 5,764.29 lbs
Largest Individual CAP CO 67.68 tons
Total CAP Emissions 151.70 tons
Total TAP Emissions 7,449.12 lbs
Total Aggregate 155.10 tons
Emissions
DAQ's Comments Regarding Inventory
Brick production for 2016 was down 10.1 percent from the brick production in 2015 and that accounts for the majority of percent
change for the pollutants emitted in 2016. Kiln 4 was tested on September 24,2015 for compliance with the 1120)brick MACT an(
the test established new emission factors for HCL and HE The test was approved by SSCB on July 11,2016. The emission
inventory submittal for 2016 did not reflect these new emission factors for HCL and HF so those have been corrected as part of the
DAQ review process. The new emission factors are as follows: HCL: 0.03 lbs/ton and HF:0.01 lbs/ton of fired brick. The percent
change in total fluorides is due to the new emission factor for HF and the percent change in Hexane,n-is due to the rotary sand
dryer operation and then the emission was only 0.5 pounds with a deminimus value for hexane,n-of 100 pounds,the facility did not
have to even report the pollutant.This would also be true for dibutylphthalate,styrene,and toluene.
l0/05/2017 Page 4 of 4

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2016 CALENDAR YEAR EMISSIONS INVENTORY
General Shale Brick, Inc. - Moncure, NC Facility
General Shale Brick
Building The American Dream'
June 2017
Project 173401.0075
Prepared By:
TRINITY CONSULTANTS
One Copley Parkway
Suite 205
Morrisville, NC 27560
[phone]
Tinn.
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Cons] Cants
Environmental solutions delivered uncommonly well

TABLE OF CONTENTS
SECTION 1: NCDAQ CY 2016 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
Dryers for 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 2016 Emissions Inventory
Trinity Consultants

jWood Fuel/Sawdust System(New) ................................................................................................................................................16
ClayHandling Equipment....................................................................................................................................................................20
IntersiteConveyer.................................................................................................................................................................................21
BrickTexturing......................................................................................................................................................................................23
CoatingsDryer.........................................................................................................................................................................................24
VacuumSystem.......................................................................................................................................................................................28
StorageTanks..........................................................................................................................................................................................29
FlyashSilo.................................................................................................................................................................................................30
CementSilo...............................................................................................................................................................................................31
i
Batch Mixer...............................................................................................................................................................................................32
Rumbler.....................................................................................................................................................................................................33
Summaryof Emissions.........................................................................................................................................................................34
FugitiveSources......................................................................................................................................................................................36
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General Shale Brick, Inc. -Moncure, NC Facility I CY 2016 Emissions Inventory
Trinity Consultants
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SECTION 1
NCDAQ CY 2016 EMISSION INVENTORY (AERO) FORMS
General Shale Brick, Inc. - Moncure, NC Facility I CY 2016 Emissions Inventory
Trinity Consultants

COPY of RECORD Date Submitted: 6/27/2017 12:19:02
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 2016
These forms must be completed and returned even if the facility did not oFerate or emissions were zero
The legally defined "Responsible Official" of record for your facility is Kevin Ham
This person or one that meets the definition below must sign this certification form.
The official submitting the information must certify that he/she complies with the requirements as specified in Title 15A
NCAC 2Q.0520(b)which references and follows the federal defmition.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 STATEMENTO
fl=ortanto Legally Responsible Official.read and sign gfter gll 5ubmissions aW,_�
certify that I am the responsible official for this facility,as described above, and hereby certify that the information contained
in this air emissions report, including attached calculations and documentation,is true,accurate and complete. (Subject to legal
enalities of up to$25,000 per occurrence and possible imprisonment as outlined in G.S.§143-215.3(a)(2))
Responsible Official's Signature Below use blue ink): Date Signed: C,(a�J 1
Printed Name: Kevin Ham
Si afore:
This form applies to Title V facilities.If this facility is not classified as Title V,please telephone your regional office Emission
Inventory contact at once for proper forms.
Email address of Responsible Official: [e-mail]
Information on this Form cannot be held confidential
COPY of RECORD Date Submitted: 6/27/2017 12:19:02 1

i
_ COPY Of RECORD Date Submitted: 6/27/2017 12:19:02
As entered in HERO
Facility Name: General Shale Brick,Inc.—Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit: 04384
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
Listing of Emission Sources and Control Devices on Permit. See instructions
ES ID on Air ES Description CS ID CS Description CD ID's
Permit
Batch mixer(39.97 tons per one bagfilter(535 sgaure
ES—BP—BM hour capacity) CS-12 feet of filter area), CD—BP—BH1
ES—BP—CS Cement silo(10 tons per hour CS-13 one bin vent filter(227 CD—BP—BV2
capacity) square feet of filter area),
IES—BP—FAS Flyash silo(11 tons per hour CS-14 one bagfilter(535 sqaure CD—BP—BHl
capacity) feet of filter area),
Natural gas—fired rotary drum
IES—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,
IES—CR5 CS-19 area),bagfilter(4,062 square
1 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
ES—CR6 Texturizing operation for Line square feet of filter CS-19 area),bagfilter(4,062 square CD—CR6BF, CD—CR7BF1,
2 CD—CR7BF2, CD—CR7BF3
feet of filter area),bagfilter
l (3,040 square feet of filter
area),
-� bagfilter(6,096 square feet
of filter area),Bagfilter(6,096
Texturizing operation for square feet of filter CD—CR6BF, CD—CR7BF1,
ES—CR7 Lines 3 and 4 CS-19 area),bagfilter(4,062 square 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
IES—Coal—CC Coal crusher CS-18 bagfilter(air to cloth ration CD—Coal—CC
of 4.7 to 1),
ES—Kl Wood/natural gas—fired tunnel CS-8 Two Simple cyclones(89 CD—Cl, CD—C2
I brick kiln(20.3 million Btu inches.in diameter)
- 2 -

t
per hour heat input and 13.7
tons per hour fired brick
-� production rate) [2D .1109
Case By Case MACT]
r I Wood/natural gas—fired tunnel
brick kiln(20.3 million Btu .
ES—K2 per hour heat input and 13.7 CS-8 Two Simple cyclones(89 CD—CI, CD—C2
tons per hour fired brick inches in diameter)
production rate) [21) .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
I kiln(25.9 million Btu per hour
heat input and 20.55 tons per'
hour maximum fired brick
j production rate) [2D .1109
ES—K3K Case By Case MACT]AOS— CS-15 dry limestone adsorber, CD—K3DLA
Coal/Natural
1 gas/propane—fired brick tunnel
kiln(25.9 million Btu per hour
heat input and 20.55 tons per
I hour maximum fired brick
production rate) [2D .1109
Case By Case MACT]
Natural gas/propane—fired
IES—K4131 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)
INatural 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
_I kiln(25.9 million Btu per hour
heat input and 20.55 tons per
hour maximum fired brick
production rate) [21) .1109
I Case By Case MACT]AOS—
j Coal/natural
gas/propane—fired brick tunnel
I . 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—CI, 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—DC I, CD—SD—DC2,
IES—WFS—SD—CV1 Transfer screw conveyor CS-17 8.06 to 1),cyclone(42 inches CD—WFS—SD—CYC,
in diameter),bin vent filter(air CD—SD—BV1,CD—SD—BV2
to cloth ratio of 4.44 to 1),bin
i vent filter(air to cloth ratio of
4.44 to 1),
dust collector(air to cloth
ratio of 8.17 to 1),dust
-I collector(air to cloth ratio of CD—SD—DC I, CD—SD—DC2,
IES-WFS—SD—CV2 Screen feed screw conveyor CS-17 8.06 to 1),cyclone ne n inches CD—WFS—SD—CYC,
in diameter),bi n vent t filter(air CD—SD—BV1, CD—SD—BV2
to cloth ratio of 4.44 to 1),bin
vent filter(air to cloth ratio of
4.44 to 1),
dust collector(air to cloth
ratio of 8.17 to 1),dust
I collector(air to cloth ratio of CD—SD—DC I, 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),
idust collector(air to cloth
ratio of 8.17 to 1),dust
collector(air to cloth ratio of CD—SD—DC I, CD—SD—DC2,
IES—WFS—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
I ratio of 8.17 to 1),dust
collector(air to cloth ratio of CD—SD—DC1, CD—SD—DC2,
ES—WFS—SD—BM 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—DC I, CD—SD—DC2,
06 to 1)
,cyclone 8x8 screen CS-17 8. 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—SC2 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
I ratio of 8.17 to 1),dust
collector(air to cloth ratio of
806 to 1)cyclone(42 inches CD—SD—DC1, CD—SD-DC2;
.
ES—WFS—SD—SDS Sawdust silo CS-17 CD—WFS—SD—CYC
in diameter),bin vent filter(air CD—SD—BV 1 CD—SD—BV2
to cloth ratio of 4.44 to 1),bin '
vent filter(air to cloth ratio of
4.44 to 1),
dust collector(air to cloth
I ratio of 8.17 to 1),dust
collector(air to cloth ratio of CD—SD—DCI, CD—SD—DC2,
ES- FS—SD—SH Surge hopper CS-17 n di to 1),cycn e n inches
W i CD—WFS—SD—CYC,
n di vent t 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]
IF—CH—Cl One impact crusher[NSPS
000]
F—CH—CFC Cape Fear conveyor[NSPS
000]
F-CH—FC Feed conveyor[NSPS 000]
F—CH—FS 1 Finishing screen[NSPS 000]
F—CH—FS2 Finishing screen [NSPS 000]
F—CH—FS3 Finishing Screen [NSPS -
000]
;F—CH—FS4 Finishing screen [NSPS 000]
-F—CH—HI Hammermill [NSPS 000]
_F—CH—H2 Hammermill [NSPS 000]
F—CH—HFC 1 Hammermill Feed Conveyor
[NSPS 000]
5

- -F—CH—HFC2 Hammermill Feed Conveyor
[NSPS 000]
F—CH—P 1 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—SS 1 Scalping screen [NSPS 000]
F—CH—SS2 Scalping Screen [NSPS 000]
I Scalping conveyor[NSPS
F—CH—SSFC 000]
F—CH—T1 Tailings conveyor[NSPS
000]
F—CH—T2 Tailings conveyor[NSPS
000]
F—CH—TC1 Trampolin Conveyor[NSPS
000]
F—CH—TC2 Trampolin_Conveyor[NSPS
000]
IF—FC4 Finishing conveyor#4 [NSPS_
000]
F—FC5 Finishing conveyor#5 [NSPS
000]
F—FS 1 Single deck screen [NSPS
000]
F—FS2 Single deck finishing screen
[NSPS Subpart 000]
F—FS3 Finishing screen[NSPS 000]
iF—FS4 Finishing screen [NSPS 000]
- IF—FS5 Finishing screen
F—FS6 Finishing screen
i
'F—FS7 Finishing screen
F—FS8 Finishing screen
.F—FS9 Finishing Screen
IF—PC Primary crusher[NSPS 000]
F—SGS Secondary crusher[NSPS
000]
IF—SS 1 Scalping Screen[NSPS 000]
6

F—SS2 Scalping Screen[NSPS 000]
I—ES—KID1 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—C1 Conveyor(coating operation)
IES—F—CO—C2 Conveyor(coating operation)
IES—F—CO—C3 Conveyor(Coating operation)
IES—F—CO—C4 Conveyor(Coating operation)
IES—F—CO—CS Conveyor(coating operation)
IES—K4F.1 Box feeder for Line 4
IES—K4F.2 conveying system for line 4
IES—K417.3 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
FIES—VS2 CS-10 feet and 297 square feet of CD—VS1,CD—VS2
vacuuming system filter area)
Hi—Vac vacuum.system for
- 'IES—VS3 Kiln 3
IES.—VS4 package—type kiln car
vacuuming system
IES—VSS
1
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
IIS-4 handling operation for Kiln 3
and 4
IS-7.1 Sand coating pile
IS-7.2 Sand coating pile
IS-7.3 Sand coating pile
IS-7.4 Sand coating pile
IS-7.5 Sand coating pile
IS-7.6 Sand coating pile
IS-7.7 Conveyor
IS-7.8 Conveyor
IS-8.1 Kiln 3 storage pile
IS-8.2 Kiln 3 box feeder
IS-8.3 Kiln 3 storage bin
IS-8.4 Kiln 3 conveyor
IS-8.5 Kiln 3 conveyor
IS-8.6 Kiln 3 conveyor
IS-8.7 Kiln 3 conveyor
IS-8.8 Kiln 3 conveyor
IS-8.9 IKiln 3 conveyor
8

i
COPY of RECORD Date Submitted: 6/27/2017 12:19:02
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
f DES Group ID *ES ID *OS ID *OS Description
GR12 ES-K3Dl,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-SCI, 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
-I G-66 ES-K1,ES-K2,ES-WD1,2 14 Wood/natural gas-fired brick kilns
f and green brick dryer(Cape Fear)
I G-69 ES-CR5,.ES-CR6,ES-CR7 37 Texturizing Operations
G-70 IES-VS1,IES-VS2 34 Vacuum System
F-C-CFBH,F-SS2,F-FC4,F-FC5,
I G-71
F-FS1,F-FS2,F-FS3,F-FS4,F-FS5, Primary Clay Grinding and� F-FS6,F-FS7,F-FS8,F-FS9,F-PC, 31 Screening Operation
F-SS1
G-72 I=ES-K1D1, I-ES-K2D1 15 Dryers associated with Kilns 1 and
2
F-CH-BC,F-CH-C 1,F-CH-CFC,
F-CH-FC,F-CH-FS 1,F-CH-FS2,
}} F-CH-FS3,-F-CH-FS4,F-CH-H1,
F-CH-1-12,F-CH-HFC1,F-CH-HFC2;
~I G-132 F-CH-PI,F-CH-P2,F-CH-RC, NONE NONE
! F-CH-SFCI,F-CH-SFC2,F-CH-SFC3,.
F-CH-SFC4,F-CH-SS1,F-CH-SS2,
F-CH-SSFC,F-CH-T1,F-CH-T2,
F-CH-TC1,F-CH-TC2
i
G-135 ES-K4D1,ES-K4D2,ES-K4D3 29 Natural gas/propane-fired dryers
L 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-K417.3,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—TI,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
ES—CD-8 6 Rotary sand drum dryer(3.45 tons
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
ES—K4K 21 Coal/Natural gas/Propane—fired
kiln#4
ES—RUMBLE 36 Rumbler tumbles blocks in a
rotating drum in order to create an
ES—SS NONE NONE
F—SGS NONE NONE
lI I—F—Coal—CH NONE NONE
I—F—Coal—CP NONE NONE
I—F—SSC NONE NONE
IES—SD NONE INONE
IS-14.15A 19 IPropane Vaporizer
_ 10

Z)
COPY of RECORD Date Submitted: 6/27/2017 12:19:02
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 2016
1. Emission Source ID (from permit) or Group GR12 consisting of ES—K3D1,ES—K3D2, ES—K3D3
Emission Source Group ID
2. Emission Source Description: Natural gas/propane—fired dryers at Brickhaven Plant
}
53. Operating Scenario ID/Description: OS—20/Natural gas/propane—fired dryers for Kiln 3
SCC Number/Description: 3050035l/Brick Manufacture—Dryer;Brick Dryer: Heated With Waste Heat
f And Supplemental Gas Burners
5. Throughputtunits in 2016:
(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):
3. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
i
-J.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID. ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
ERP for ES—K3K,
I EP—K3 VERTICAL STACK 35 4.92 99.95 33.79 38544.24 ES—K3D1 AND
ES-K3D2
ti
1.1.

Operating Scenario: OS—20 Emission Source/Group ID: GR12
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% 25% une—Aug. 25% Sept.—Nov. 25%
016 �arch—May
16 2016 2016
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions) all controls
2016
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAAQS) Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2016
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP CAS Emissions Emission
Control
I
Pollutants (In HAP/TAPS Estimation Efficiency Factor Emission
(see instructions EF Control
) Method Code I Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
J 2016
12

9
DID 44�
COPY of RECORD Date Submitted: 6/27/2017 12:19:02
As entered in AFRO
Facility Name: General Shale Brick,Inc.—Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit : 04384
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
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—SC I,ES—WFS—SD—SC2, ES—WFS—SD—SDS,
ES—WFS—SD—SH
2. Emission Source Description: Wood Fuel/Sawdust System
- 3. Operating Scenario ID/Description: OS—30/Wood Fuel/Sawdust System
4. SCC Number/Description: 30500305Brick Manufacture—Material Prep ; Raw Material Handling and
Transferring
_'5. Throughput/units in 2016:
(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):
3' Control Device Information
Order CS-11) CD ID Control Device Description
as listed inpen-nit)
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—BV 1 One bin vent filter 4.44:1 air to cloth ratio
5 CS-17 CD—SD—BV2 One bin vent filter 4.44:1 air to cloth ratio
- r
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/see) Rate(Acfm)
Rectangle(L x W)
(in 0.1 feet)
13

P—SD—BV1 VERTICAL STACK 20 0.5 72 33.95 400 Bin vent on sawdust
silo
Dust Collector on
yste
-CEP—SD—DC2 VERTICAL STACK 20 1 72 49.76 2345 S el Sawdust
System Screens
Conveyors
P—SD—BV2 VERTICAL STACK 20 0.5 75 33.95 400 Bin Vent on Surge
Hopper
Dust Collector on
jEP—SD—DC1 VERTICAL STACK 20 1 72 44.56 2100 Woodf iel Sawdust
I System Screens
Conveyors
f
I
it
14

Operating Scenario: OS—30 Emission Source/Group ID: GR21
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year-2016)
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 25% 25% une—Aug. 25% �016
ept.—Nov. 25%
�2016 �arch—May
16 2016
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
IEmissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
{ Criteria Emissions— Emission Control
I
Pollutant Criteria Estimation Efficiency Emission o� Code Pollutants Method Code (Net after Factor Ef Control
Pollutaantnt s
(Tons/Year) (See Instructions) all controls)
2016
CO CO 08
NOx NOx 08
TSP ` TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP CAS Emissions Emission .
Control
Pollutants (In HAP/TAPS Estimation EfficiencyEmission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (PoundsNear) See Instructions) et after all controls)
2016
i
15

RUMAD Z)
COPY of RECORD Date Submitted: 6/27/2017 12:19:02
As entered in AFRO
'Facility Name: General Shale Brick,Inc.—Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit : 04384
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
1. Emission Source ID (from permit) or Group GR22 consisting of IES—VS3, IES—VS4, IES—VS5
Emission Source Group ID
2. Emission Source Description: Vacuum Systems—Brickhaven
3. Operating Scenario ID/Description: -OS— 35/Vacuum Systems—Brickhaven
4. SCC Number/Description: 30500317/13rick Manufacture—Material Prep ; Raw Material Unloading
5. Throughput/units in 2016: 1500 HR/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):
i
.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 e ry 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
)
(in 0.1 feet)
EP—VS3 DOWNWARD—FACING VENT 1 3 72 3.3 1400 Emission Point for
IES—VS3
EP—VS4 DOWNWARD—FACING VENT 1 3 72 3.3 1400 Emissions point
for IES—VS4
I EP—VS5 DOWNWARD—FACING VENT 1 3 72 3.3 1400 Emission point for
IES—.VS5
16

V
Operating Scenario: OS—35 Emission Source/Group ID: GR22
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
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 25% arch—May 25% une—Aug. ° �016
ept.—Nov. °
2016 016 �2016 25/O 25/o
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
IEmissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency
Emission
(NAAQS) Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2016
CO CO 08
NOx NOx - 08
TSP TSP 0.09 08
PM10 PM10 0.09 08
PM2.5 PM2.5 0.09 08
S02 S02 08
VOC VOC 08
HAP/TAP Emissions Emission Control
Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code Factor
Alphabetical,Order) (Pounds/Year) (Net after all controls)
See Instructions
2016
17

V
DID No-r dPEP_,qT
COPY of RECORD Date Submitted: 6/27/2017 12:19:02
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 2016
1. Emission Source ID(from permit)or Group G-66 consisting of ES—K1,ES—K2, ES—WD1,2
Emission Source Group ID
2. Emission Source Description: Two Wood/natural gas—fired brick kilns and green brick dryer
I
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 2016:
(e.g.production or fuel use):
16. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-8 CD—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 entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume-Flow ERP Description
(in feet) Circle(enter ft (F) (Feettsee) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
ERP for ES—Kl,
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—SD1
18

Operating Scenario: OS— 14 Emission Source/Group ID: G-66
-110.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
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 +Dee 25% arch—May 25% une—Aug. 25% �016
ept.—Nov. 25%
2016 2016 �016
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 y Ef Control .
Pollutants Method Code (Net after Factor
TonslYear) (See Instructions all controls
- 2016
Criteria Emissions- Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission Ef Control
Code
Pollutants Method
o Code (Net after Factor
Pollutants
(Tons/Year) (See Instructions) all controls)
2016
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP CAS Emissions Emission
Control
HAP/TAPS Estimation Emission
Pollutants (In
(see instructions) Efficiency Method Code Factor EF Control
Alphabetical Order) (Pounds/Year) (Net after.all controls)
See Instructions
2016
i
20

COPY of RECORD Date Submitted: - 6/27/2017 12:19:02
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 2016
11. 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
13. Operating'Scenario ID/Description: OS—37/Texturizing Operations
4. SCC Number/Description: 30500397Brick Manufacture; *Other Not Classified
5. Throughput/units in 2016: 118725 TON/yr-
I(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
4! 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 II) ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
IRectangle(L x W)
in 0.1 feet)
EP—CR6 HORIZONTAL STACK 20 1 72 21.2 999.02 1 ERP for ES—CR-6
EP—CR7 1HORIZONTAL STACK 20 1 72 21.2 999.02 ERP for ES—CR-7
21

;Operating Scenario: OS —37 Emission Source/Group ID: G-69
l
J0.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
Hours per Day ( 24 ) Days per-Week ( 7 ) Weeks per Year ( 52 )
G11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
i
12. Seasonal Periods Percent Annual Throu h ut:
Jan—Feb +Dec 25% 25% une—Aug. 25% �016
ept.—Nov. 25%
016 �arch—May
16 016
13. Actual Emissions per Pollutant Listed
;Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAAQS) Code Pollutants Method Code (Met after Factor Ef Control
Pollutants (Tons/Year) (See Instructions) all controls)
i
2016
CO CO 08 0
' NOx NOx 08 0
TSP TSP 0.21 08 99 0.0036 AFTER
PM10 PM10 0.21 08 99 0.0036 AFTER
PM2.5 PM2.5 0.21 08 99 0.0036 AFTER
S02 S02 08 0
VOC VOC 08 0
HAP/TAP CAS Emissions Emission Control
Pollutants (In HAP/TAPS Estimation Emission EF Control
(see instructions) Method Code Efficiency Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2016
i
7
1 .
f
i
i
J 22

COPY of RECORD Date Submitted: 6/27/2017 12:19:02
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 2016
1. Emission Source ID (from permit) or Group G-70 consisting of IES—VS 1,IES—VS2
Emission Source Group ID
2. Emission Source Description: Vacuum System
3. Operating Scenario ID/Description: OS—.34/Vacuum System
SCC Number/Description: 30500317Brick Manufacture—Material Prep;Raw Material Unloading
i
5. Throughput/units in 2016: 1300 HR/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) % Sulfur %Ash Heat Content
-) Btu/units
_17. 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 en lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP
(in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm). Description
Rectangle(L x
j . )
(in 0.1 feet)
_.,EPVS2 DOWNWARD—FACING VENT 1 3 72 3.3 1400 ERP for
CD—VS2
�I EPVS 1 DOWNWARD—FACING VENT 1 3 72 3.3 1400 ERP forCD—VS 1
f
23

+Operating Scenario: OS—34 Emission Source/Group ID: G-70
,10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% 25%25% une—Aug. 25% Sept.—Nov. 25%
016 016 2016 016
'13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAAQS) Code Pollutants Method Code (Net after Factor Ef Control
I,f
Pollutants (Tons/Year) (See Instructions) all controls)
2016
CO CO 08 0
NOx NOx 08 0
TSP TSP 0.08 08 99.9 AFTER
PM10 PM_10 0.08 08 99.9 AFTER
PM2.5 PM2.5 0.08 08 99.9 AFTER
S02 S02 08 0
VOC VOC 08 0
HAP/TAP Emissions Emission
Control
CAS Estimation Emission
Pollutants (in see instructions HAP/TAPS Efficiency EF Control
( ) Method Code Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2016
M
- 24

COPY of RECORD Date Submitted: 6/27/2017 12:19:02
{ 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
I
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
Emission Source ID(from permit)or Group G-71 consisting of F—C—CFBH,F—SS2,F—FC4,F—FC5,F—FS 1,
',mission Source Group ID F—FS2,F—FS3,F—FS4,F—FS5,F—FS6,F—FS7,F—FS8,F—FS9,F—PC,F—SSI
L. Emission Source Description: Clay Handling Equipment
3. Operating Scenario ID/Description: OS—3I/Primary Clay Grinding and Screening Operation
f
1. SCC Number/Description: 30500302/Brick Manufacture—Material Prep ;Raw Material Grinding
Screening
5. Throughput/units in 2016: 107146 TON/yr -
"e.g.production or fuel use):
i. 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):
1. Control Device Information :None
I 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)
IRectangle(L x W)
in 0.1 feet)
FUGITIVE(NO ERP for Fugitive
EP—FG STACK 1 72 Area= 1
sources
I
i
i
_ 25

,Operating Scenario: OS—31 Emission Source/Group ID: G-71
J0.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
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:
Jan—Feb +Dec 25% 25% une—Aug. 25% �016
ept.—Nov. 25%2016 �arch—May
16 �016
13. Actual Emissions per Pollutant Listed
-Attach calculations and documentation of emission factors or other estimation methods used.
IEmissions— Emission Control
GHG GHG Estimation Efficiency Emission
Pollutants CAS pollutants Method Code (Net after Factor Ef Control
Tons/Year See Instructions all controls
2016
i Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAAQS) y Ef Control
Pollutants Code Pollutants Method Code (Net after Factor
I (Tons[Year) (See Instructions) all controls)
k 2016
CO CO 08
NOx NOx 08
TSP TSP 1.4 08 0.02604 .
PM10 PM10 0.15 08 0.002791
PM2.5 PM2.5 0.13 08 0.002374
S02 S02 08
VOC VOC 08
HAP/TAP Emissions Emission Control
I Pollutants .(In CAS HAP/TAPS- Estimation Efficiency Emission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2016
l
i
26

COPY of RECORD Date Submitted: 6/27/2017 12:19:02
As entered in AFRO
''Facility Name: General Shale Brick,Inc. —Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit: 04384
Moncure,NC 27559 County : Chatham
DAQ Region :RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory Calendar Year 2016
L Emission Source ID (from permit) or Group G-72 consisting'ofI—ES—K1D1,I-ES—K2131
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
. SCC Number/Description: 30500305Brick Manufacture—Material Prep;Raw Material Handling and
Transferring
5. Throughput(units in 2016:
(e.g.production or fuel use):
S. 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):
3. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed in ermit
F
J.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)-
ectangle(L x W)
(in-0.1 feet)
j FUGITIVE(NO ERP for Fugitive
EP—FG 1 STACK 1 72 Area= sources
27

!Operating Scenario: OS — 15 Emission Source/Group ID: G-72
J0.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% 25% une—Aug. 25% ept.—Nov. 25%
016 �arch—May
16 �016 �016
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency
Emission
(NAA Code Pollutants Method Code (Net after Factor Ef Control
Pollutants (Tons/Year) (See Instructions) all controls)
2016
CO CO 08
NOx NOx 08
TSP TSP. 08
PM10 PM,10 08
PM2.5 PM2.5 08
S02 S02 08
- VOC VOC 08
Emission
t HAP/TAP CAS Emissions Control
I Pollutants (In HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code Factor
'Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2016
28 _

f -
_ COPY of RECORD Date Submitted: 6/27/2017 12:19:02
As entered in HERO
!Facility Name: General Shale Brick,Inc.—Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit: 04384
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
1. Emission Source ID (from permit) or Group G-135 consisting of ES—K4D1,ES—K4D2,ES—K4D3
,Emission Source Group ID
2. Emission Source Description: Natural gas/propane—fired dryers at Brickhaven Plant
i
13. Operating Scenario ID/Description: OS—29/Natural gas/propane—fired dryers for Kiln-4
14. SCC Number/Description: 30500351/13rick Manufacture—Dryer; Brick Dryer: Heated With Waste Heat
And Supplemental Gas Burners
5. Throughput/units in 2016: 118725 TON/yr
(e.g.production or fuel use):
,6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
I(%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(ERPI 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 Vie
in 0.1 feet)
EP—K4D1 VERTICAL STACK 34.78 4.92 99.95 33.79 38544.24 Brick Dryers on
Kiln 4
i
i
29

!Operating Scenario: OS—29 Emission Source/Group ID: G-135
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
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% �016
ept.—Nov. 25%
016 016 �016
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
i
2016
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(hTAA Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2016
CO CO 18.4 08 0.31
NOx NOx 5.82 08 0.098
TSP TSP 11.1 08 0.187
PM10 PM10 11.1 08 0.187
PM2.5 PM2.5 11.1 08 0.187
S02 S02 08
VOC VOC 1.78 08 0.03
HAP/TAP Emissions Emission Control
Pollutants (In CAS HAP/TAPS Estimation Emission
Efficiency EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) See Instructions) (Net after all controls)
2016
I
t
I
30

COPY Of RECORD Date Submitted: 6/27/2017 12:19:02
As entered in HERO
Facility Name: General Shale Brick,Inc.—Moncure Facility Facility ID : 1900009
_ 300 Brick Plant Road _ Permit : 04384
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
1. Emission Source ID (from permit)or Group G-144 consisting of IES—T1,IES—T2,IES—T3,IES—T4,IES—T5
Emission Source Group ID
2. Emission Source Description: Storage tanks
3. Operating Scenario ID/Description: OS— 18/Storage tanks
:4. SCC Number/Description: 39090004/Fuel Storage—Fixed Roof Tanks ;Distillate Oil(No.2): Working
Loss -
• i r
'5. Throughput/units in 2016: 81935 GAL/yr "` + l'�3+ 1�¢f'v�,�a L °' •
(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):
3. 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 EPP use additional entry lines :
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
I (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
31

Operating Scenario: OS— 18 Emission Source/Group ID: G-144
l0.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
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%
016 1 016 016 016
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
} Emissions— Emission Control
GHG on GHG Estimation Efficiency Emission
Pollutants CAS y Ef Control
Pollutants Method Code (Net after Factor
Tons/Year See Instructions all.controls
2016
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)
2016
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 U1638
HAP/TAP CAS Emissions Emission Control
I
Pollutants (In HAP/TAPS Estimation Emission(see instructions) Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) See Instructions) (Net after all controls)
2016
- I
32

Vol'
COPY of RECORD Date Submitted: 6/27/2017 12:19:02
As entered in AFRO
Facility Name: General Shale Brick,Inc.—Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit: 04384
Moncure,NC 27559 County : Chatham
DAQ Region:RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality _
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
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 ED/Description: OS—26/Batch Mixer
4. SCC Number/Description: 31299999/Miscellaneous Machinery;Other Not Classified
5. Throughputtunits in 2016:
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) ro Sulfur %Ash 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 in permit
1 .CS-12 CD—BP-131­11 One ba filter 535 s aure feet of filter area
.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)
BMX VERTICAL STACK 44.95 1.312 72.05 40.02 3246.27 Batch Mixer
Ba house
i
G
33

;Operating Scenario: OS—26 Emission Source/Group ED: ES—BP—BM
- 10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
-I;11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% 25% une—Aug. 25% �016
ept.—Nov. 25%
2016 �arch—May
16 2016
13. Actual Emissions per Pollutant Listed : i
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAAQS) Code Pollutants Method Code (Net after Factor Ef Control
Pollutants (Tons/Year) (See Instructions) all controls)
i
2016
CO CO 08
NOx NOx 08
TSP TSP 08 -
PM10 PM10 08
PM2.5. PM2.5 08
902 S02 08
VOC VOC 08
HAP/TAP CAS Emissions Emission Control
Pollutants (In HAP/TAPS Estimation Emission EF Control
see instructions Efficiency
Alphabetical Order) ( ) (Pounds/Year) Method Code (Net after-all controls) Factor
See Instnuctions
2016
J
34

V,
COPY of RECORD Date Submitted: 6/27/2017 12:19:02
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
i -
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
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 2016:
,(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-13 CD—BP—BV2 one bin vent filter 227 square feet of filter area
J.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)
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 2016)
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:
016an—Feb +Dec 25% �016 arch—May 25% 016—Aug. 25% S0ept6.—Nov. 25%
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission
Pollutants Pollutants Method Code (Net after Factor Ef Control
Tons/Year See Instructions all'controls
2016
Criteria Emissions— Emission Control
f (NAAQS) Pollutant Criteria Estimation Efficiency Emission
Pollutants Code Pollutants Method Code (Net after Factor Ef Control
(Tons/Year) (See Instructions) all controls)
2016
CO CO '08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC -VOC 08
HAP/TAP CAS Emissions Emission
Control HAP/TAPS Estimation Emission
Pollutants (In
I (see instructions) Efficiency
Alphabetical Order Method Code Ef EF Control
p ) (Pounds/Year) See Instructions (Net after all controls) Factor
2016
�f
36

COPY Of RECORD Date Submitted: 6/27/2017 12:19:02
As entered in AERO
—Facility Name: General Shale Brick,Inc. —Moncure Facility Facility ID : 1900009
JI 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 2016
Emission Source ID(from permit)or ES—BP—FAS
.,mission Source Group ID
2. Emission Source Description: Flyash silo(11 tons per hour capacity)
S. Operating Scenario ID/Description: OS—28/Flyash Silo
1. SCC Number/Description: 31299999/Miscellaneous Machinery ;Other Not Classified
5. Throughput/units in 2016:
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed in ermit
1 CS-14 CD—BP—BH1 One ba filter 535 s aure feet of filter area
).Emission Release Point RP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L.x W)
in 0.1 feet)
j FLY VERTICAL STACK 44.95 1.15 72- 60 3739.28 Flyash Silo Bin
Vent
37

- f
Operating Scenario: OS—28 Emission Source/Group ID:ES—BP—FAS
--,10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
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 25a�o arch—May 25"�a une—Aug. 25% Sept.—Nov. 25%
2016 016 016 016
13. Actual Emissions per Pollutant Listed-:
-Attach calculations and documentation of emission factors or other estimation methods used.
IEmissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
( (NAAQS) Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
- _ (Tons/Year) (See Instructions) all controls)
j 2016
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC. 08
HAP/TAP Emissions Emission. Control
CAS Estimation Emission
IPollutants (In (see instructions) HAP/TAPS Method Code Factor Efficiency - EF Control
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2016
-�r
38

COPY of RECORD Date Submitted: 6/27/2017 12:19:02
As entered in HERO
Facility Name: General Shale Brick,Inc. —Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit : 04384
Moncure,NC 27559 County :.Chatham
DAQ Region :RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
-1. Emission Source ID (from permit) or ES—CD-8
Emission Source Group ID
2. Emission Source Description: Natural gas—fired rotary drum coatings dryer(250,000 Btu per hour heat input;
3.45 tons per hour drying capacity)
3. Operating Scenario ID/Description: OS—6/Rotary sand drum dryer(3.45 tons per hour)
1. SCC Number/Description: 30500301/13rick Manufacture Dryer;Raw Material Drying
>. Throughput/units in 2016: 0.255 E6FT3/yr
(e.g.production or fuel use):
�. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
3. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
►.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
t '
39

Operating Scenario: OS—6 Emission Source/Group ID: ES—CD-8
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52
11.Typical Start& End Times For Operating Scenario: Start: 0 End: 2359
i
12. Seasonal Periods Percent Annual Throu h ut:
Jan—Feb +Dec 25% . 25% une—Aug. 25% Sept.—Nov. 25%
016 �arch—May
16 2016 2016
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission - Control
- (NAAQS) Pollutant Criteria Estimation Efficiency Emission Ef Control
Pollutants Code Pollutants Method Code (Net after Factor
7 (Tons/Year) (See Instructions) all controls)
I 2016
CO CO 0.01 08 84
NOx NOx 0.01 08 100
TSP TSP 0.03 08
PM10 PM10 0.03 08,
PM2.5 PM2.5 0.03 0.8
S02 S02 0 08 0.6
VOC VOC 0 08 5.5
Emissions Emission Control
HAP/TAP CAS Estimation Efficienc Emission
Pollutants (In Alphabetical Order) (see instructions) HAP/TAPS Method Code (Net after all Factor EF Control
(Pounds/Year)
See Instructions controls)
2016
Benzene 71-43-2 0.00054 08 0.0021
Dichlorobenzene 14— 106-46-7 0.00031 08 0.00123
Formaldehyde 50-00-0 0.01912 08 0.075
Hexane,n 110-54-3 0.459 08 1.8
Lead Unlisted Compounds
(Specify and Component of PBC—Other 0.00013 08 0.0005
PBC
_!Naphthalene(Component of 91-20-3 0.00016 08 0.00061
POMT
Selenium Compounds SEC 0.00001 08 0.000024
Toluene 108-88-3 0.00087 08 0.0034
40

COPY of RECORD Date Submitted: 6/27/2017 12:19:02
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 2016
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 2016:
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
Btu/units
i
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 30 2 75 18.56 3500 One Ba filter
i
42

Operating Scenario: OS—33 Emission Source/Group ID:ES—Coal—CC
-10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
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 +��55% ° une—Aug. ° �016
ept.—Nov. °2016 �arch—May
16 25/0 �016 25%° 25/o
13. Actual Emissions per Pollutant Listed : -
Attach calculations and documentation of emission factors or other estimation methods used.
IEmissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAAQS) Code Pollutants Method Code (Net after Factor Ef Control
. Pollutants
(Tons/Year) (See Instructions) all controls)
2016
CO CO 08
NOx NOx 08
-- TSP TSP. 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08 '.
Emission
HAP/TAP Emissions Control
CAS Estimation Emission
I Pollutants (In (see instructions) HAP/TAPS Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) See Instructions) (Net after all controls)
2016-
w
43

COPY of RECORD Date Submitted:, 6/27/2017 12:19:02
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 2016
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— 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 2016:
;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)
1.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
I_ (in feet) Circle(enter ft (F) (Feet/see) 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
J ES—K3D2
44

Operating Scenario: OS— 10 Emission Source/Group ID:ES—K3K
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
:Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
L Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
Jan-Feb +Dec 25% arch May 25% une—Aug. 25% Sept.—Nov. 25%
`2016 016 016 016
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
IEmissions— Emission Control
GHG GHG Estimation Efficiency Emission
Pollutants CAS Ef Control
Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission Control
Pollutant
(NAAQS) Criteria Estimation Efficiency . Emission
Pollutants
Code Pollutants Method Code (Net after Factor Ef Control
(Tons/Year) (See Instructions) all controls)
2016
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08 ,
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP CAS Emissions Emission
Control
I Pollutants (In. HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) See Instructions) (Net after all controls)
2016
_ 1
45

COPY. Of RECORD Date Submitted: 6/27/2017 12:19:02
As entered in HERO
Facility Name: General Shale Brick,Inc. —Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit : 04384
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
1. Emission Source ID (from permit)or ES—K3K
Emission Source Group ID
2. Emission Source Description: POS—Natural gas/propane—fired brick tunnel kiln(25.9 million Btu per hour
heat input and 20.55 tons per hour maximum fired brick production rate) [2D
.1109 Case By Case MACT] AOS —Coal/Natural
3. Operating Scenario ID/Description: OS—25/10/Natural gas/propane/coal—fired kiln#3
4. SCC Number/Description: 3050031 l/Brick Manufacture—Curing Firing; Curing and Firing: Gas—fired
Tunnel Kilns
5. Throughput/units in 2016:
i(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-15 CD—K3DLA Dry limestone adsorber
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entr lines :
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
j (in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm)
I
-- Rectangle(L x W)
(in 0.1 feet)
EP—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 2016)
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:
t—Feb +Dec 25% arch—May 25% une—Aug. 25% Sept.—Nov. 25%
6 016 2016 2016
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission Control
(NAAQS)- Pollutant Criteria Estimation Efficiency Emission Ef Control
Code Pollutants Method Code et after Factor
Pollutants
Pol n s (N
(Tons/Year) (See Instructions) all controls)
2016
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02. 08
VOC VOC 08
HAP/TAP CAS Emissions Emission
Control
Pollutants (In HAP/TAPS Estimation Emission
ffi
Method Code Efficiency Factor EF Control
(see instructions)
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2016
47

COPY of RECORD Date Submitted: 6127/2017 12:19:02
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 2016
it. Emission Source ID (from permit) or ES—K4K
Emission Source Group ID
2. Emission Source Description: POS—Natural gas/propane—fired brick tunnel kiln(25.9 million Btu per hour
heat input and 20.55 tons per hour maximum fired brick production rate) [2D
.1109 Case By Case MACT] AOS—Coal/natural
3. Operating Scenario ID/Description: OS—2 1/Coal/Natural gas/Propane—fired kiln#4
4. SCC Number/Description: 30500311Brick Manufacture—Curing Firing; Curing and Firing: Gas—fired
Tunnel Kilns
10- a 4fifca s 00 d
5. Throughput/units in 2016: 118725 TON/yr
[e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
Btu/units
`7. Capture Efficiency
(%of Emissions from this Process Vented to Control 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 fines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
I (in 0.1 feet)
Dry limestone
iEP—K4DLA VERTICAL STACK 75.13 4.92 469 43.64 49780.13. adsorber on Kiln 4.
48

s ,
4 sd
L
os d/j C'OP
L n ee=
0
P� r
operating Scenario: OS — 21 Emission Source/Group ID: ES—K4K
S
�F ,10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
Hours per Day ( 8 ) Days per Week ( 5 ) Weeks per Year ( 52 )
0�60
y 41.Typical Start& End Times For Operating Scenario: Start: 0 End: 2359 s,
P�!
Cs, 12. Seasonal Periods Percent Annual Throu h ut:
Jan—Feb +Dec ° arch—May 25% une—Aug. ° Sept.—Nov.
25% 016 2016 25/0 2016 25%
'� �'2016
FA dsP o 0 20 Actual Emissions per Pollutant Listed
°> ' °P Attach calculations and documentation of emission factors or other estimation methods used.
�9
Emission
Poo Emissions— Estimation Control
°
` GHG GHG Method Efficiency Emission
�, �: �P
P^ O^ 60� tt` s�P/P
`P c, Pollutants CAS pollutants Code (Net after Factor f Control
(Tons/Year) (See all controls)I
Instructions
2016
,sr, di.
Qre Spa a°c O� cp L p r
�I °� L IC`'Jj, pip Pad
ram^ Emission
d 8 0° � Emissions— Estimation Control
��' 9s� �''�o, °�L L °,cam % ' i Criteria Pollutant Criteria Method Efficiency Emission
�9 °zsPr F� �J'6Pf 0o�j l+r' (NAAQS) Code Pollutants Code (Net after Factor Ef Control
Pollutants
G r ° y (Tons/Year) (See all controls)
Instructions)
2016
L� °o CO CO 49.27080
2- ,� NOX In ° NOx 20.78 08 0
0 y �
.e oOo°' e� ` ° 0 20� '� TSP TSP 41.19 08 0
A'1s a PM10 41.19 08 0
PM10
PM2.5 41.19 08 0
PM2.5
F9 L o� �9 6B 9 p s` S02 SO2 0.68 08 0
VOC VOC 1.43 08 0
8
T A Emission
Emissions Estimation Control
�Q+ HAP/TAP CAS Method Efficiency Emission
HAP/TAPS EF Control
fee °4e °`°any Pollutants (in Alphabetical Order) (see instructions) (Pounds/Year) Code (Net after all Factor
d� Py (See controls)
@� o9ss I Instructions
A 1 2016
Arsenic Unlisted Compounds ( ASC—Other 3.68048 08 0 0.000031
S ecif Com onent of ASC AFTER
�'O!) Benzene 71-43-2 344.3025 08 0 0.0029 AFTER
-------------
Cadmium Metal (elemental 7440-43-9 1.78088 08 0 0.000015
unreacted,Component of CDC) AFTER
Chlorine 7782-50-5 154.3425 08 0 0.0013 AFTER
Chromic acid (VI) (Component of 7738_94-5 6.05498 08 0 0.000051
AFTER
SOICR6 CRC
Pi 2—eth hex 1 hthalate EHP 117-81-7 237.45 08 0 1 0.002 AFTER
Dichlorobenzene , 0— 106-46-7 56998 08 0 1 0.000048 AFTER

s
Ole
fiv
S 4�
c�
/ Q O
6Qe� ay�o aiF� 00
An v
b�Q ^c + . �c�� oa`�o�p�a.4�
Ise
Ica
�O" U ^(� � ��` �✓, ,ec`�oa�� o � � ��o �;�b `�SQvo`a'� N���Oa''° O
2Q J
Q o
'ace�5-4 SQ3
e o ♦ Sa,
o�J'
`Q�Q�� 4QFJ
a
w
�9 09 0
`e

Ethyl chloride chloroethane 75-00-3 67.67325 08 0 0.00057 AFTER
Fluorides (sum of all fluoride l8 .
compounds)
16984-48-8 .� 08 0 QrG j4,
Formaldehyde 50-00-0 19.6 08 0
Hydrogen chloride (hydrochloric 8541.75 0�
acid
7647-01-0 �'�ff-5, 08 0 DA263" AFTER
Hydrogen fluoride (hydrofluoric E1137.Z 6 0,01
^� ^�acid as mass of HF-Component of 7664-39-3 69 -4 08 90 -0-00577 AFTER
Fluorides
Lead Unlisted Compounds(Specify PBC-Other 17.80875 08 0 0.00015 AFTER
and Component of PBC
Mercury,vapor(Component of 7439-97-6 0.89044 08 0 0.0000075 AFTER
HGC
Methyl chloride 74-87-3 79.54575 08 0 0.00067 AFTER
Methyl iodide 74-88-4 11.04143 08 0 0.000093 AFTER
Naphthalene(Component of
POMT 91-20-3 7.71712 08 0 0.000065
Nickel metal(Component of NIC 7440-02-0 8.5482 08 0 0.000072 AFTER
Selenium Compounds SEC 27.30675 08 0 0.00023 AFTER
Styrene 100-42-5 2.3745 08 0 0.00002 AFTER
Toluene 108-88-3 18.996 08 0 0.00016 AFTER
�' S� ���T,t�J.ti ���'� /�Z•T/4EMEC� OPf�S 17'7C ��.
50

COPY of RECORD Date Submitted: 6/27/2017 12:19:02
As entered in AFRO
Facility Name: General Shale Brick,Inc.—Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit: 04384
Moncure,NC 27559 County: Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
L Emission Source ID (from permit)or ES—RUMBLE
Emission Source Group ID
2. Emission Source Description: Rumbler system
3. Operating Scenario ID/Description: OS—36/Rumbler tumbles blocks in a rotating drum in order to create an
4. SCC Number/Description: 30500397Brick Manufacture ; *Other Not Classified
5. Throughput/units in 2016:
'e.g.production or fuel use):
6. Fuel Information (If fuel is used) _ ro
Sulfur %Ash Heat Content
Btu/units
1. 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):
IERP 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—RUMBLE VERTICAL STACK 44.95 1.312 72.05 40.02 3246.27 Rumbler Ba house
51

Operating Scenario:OS—36 Emission Source/Group ED
ES—RUMBLE
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% 25% une—Aug. 25% �016
ept.—Nov. 25%
016 �arch—May
16 �016
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used:
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAAant Code Pollutants Method Code (Net after Factor Ef Control
Pollutants (Tons/Year) (See Instructions) all controls)
2016
' CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP CAS Emissions Emission Estimation Control Emission
Pollutants (In (see instructions) HAP/TAPS Efficiency Factor EF Control
Method Code
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2016
52

COPY Of RECORD Date Submitted: 6/27/2017 12:19:02
As entered in HERO
'Facility Name: General Shale Brick,Inc. —Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit: 04384
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2016
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: 30500397Brick Manufacture; *Other Not Classified
5. Throughputtunits in 2016:
_ `(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
{Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) (Acfm)
Rectangle(L x W)
(in 0.1 feet).
EP—FG FUGITIVE(NO 1 72 Area— I ERP for Fugitive
STACK) sources
'4
i
53

'Operating Scenario: OS— 19 Emission Source/Group ID: IS-14.15A
,10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2016)
i 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%
016 016 016 016
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG- CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2016
Criteria Emissions— Emission Control
t Pollutant Criteria Estimation Efficiency Emission
(NAAQS) Code Pollutants Method Code (Net after Factor Ef Control
Pollutants (Tons/Year) (See Instructions) all controls)
2016
CO CO 08
NOx NOx 08
TSP. TSP 08
-PNI10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP Emissions Emission
CAS Estimation Control Emission
Pollutants (In (see instructions) HAPITAPS Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) See Instructions) (Net after all controls)
2016
4
64

Facility Total CY 2016 Emissions Summary
COPY of RECORD Date Submitted: 6/27/2017 12:19:02
As entered in A►ERO
;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-2016-
Record Facility—Wide Totals From all Permitted and Non—Permitted Air Pollutant Emission Sources
Green House Gases Pollutants(GHG)
Actual Emissions Tons/Year
Pollutant CAS 2016 1 2015 1 % Change
Criteria Pollutants
Actual Emissions Tons/Year
Pollutant CAS 2016 2015 % Change
CO CO 67.68 75.31 —10.1314535%
NOx NOx 26.61 29.59 —10.070968%
PM TSP TSP 54.1 60.72 —10.902507%
PM10 PM10 52.85 58.85 —10.195413%
PM2.5 PM2.5 52.83 58.81 —10.168338%
S02 S02 0.68 .76 —10.526314%
VOC VOC 3.88 4.24 —8.490559%
Hazardous Air Pollutants HAPS and/or Toxic Air Pollutants TAPS
Actual Emissions Pounds/Year
- Pollutant CAS 2016 2015 % Change
[Pollutant Group:Arsenic Compounds (total mass of elemental AS,arsine and all inorganic compounds) Group
Sum:3.68048
-T
'Arsenic Unlisted Compounds (Specify ASC—Other 3.68048 4.09553 —10.134221%
Component of ASC
Pollutant Grou :Cadmium compound total mass inc elemental metal Group Sum:1.78088
Cadmium Metal(elemental unreacted, 7440-43-9 1.78088 198171 —10.134176%
Component of CDC
Pollutant Grou :Chromium VI Soluble Chromate Compounds(Component of CRC Group Sum:6.05498
Chromic acid(VI) (Component of °
So1CR6 CRC 7738-94-5 6.05498 6.73781 —10.134307/o
Pollutant Grou :Chromium—All/Total Inc Chromium VI categories,metal and Others Group Sum:6.05498
Chromic acid(VI) (Component of 7738-94-5 6.05498 6.73781 —10.134307%
So1CR6 CRC
Pollutant Grou :Lead and Lead compounds Grou p Sum:17.80888
Lead Unlisted Compounds(Specify PBC—Other 17.80888 19.8171 —10.133777%
55

and Component of PBC
Pollutant Grou :Mercu Compounds-all total mass, inc H Vapor Group Sum:.89044
Mercury,vapor(Component of HGC 1 7439-97-6 1 0.89044 1 .99086 -10.13463%
Pollutant Grou :Nickel Compounds, sum total mass, inc elemental Group Sum:8.5482
Nickel metal(Component ofNIC 7440-02-0 8.5482 9.51221 T -10.134451%
Pollutant Grou :Pol c clic Organic Matter(Specific Com ounds from OA PS for T Group Sum:7.71728
Naphthalene(Component of POMTV 91-20-3 7.71728 8.58747 -10.133254%
Benzene 71-43-2 344.30304 383.13079 -10.1343355%
Chlorine 7782-50-5 154.3425 171.7482 -10.13443%
Di 2-eth lhex 1 hthalate DEHP 117-81-7 237.45 264.228 -10.13443%
Dichlorobenzene , 1,4-. 106-46-7 5.69911 6.34147 -10.129509%
Ethyl chloride chloroethane 75-00-3 67.67325 75.30498 -10.134429%
Fluorides(sum of all fluoride 16984-48-8 1096.0 8060 -86.401985%
compound
Formaldehyde 50-00-0 19.61912 18.45689 6.2969956%
Hexane, n- 110-54-3 0.459 .16542 177.47552%
Hydrogen chloride(hydrochloric acid 7647-01-0 3122.4675 3474.5982 -10.134427%
I Hydrogen fluoride (hydrofluoric acid
as mass of HF-Component of 7664-39-3 685.0433 762.29778. -10.134427%
Fluorides
Methyl chloride 74-87-3 79.54575 88.51638 -10.134426%
Methyl iodide 74-88-4 11.04143 12.2866 -10.134372%
Selenium Compounds SEC 27.30676 30.38622 -10.134397%
Styrene 100-42-5 2.3745 2.64228 -10.134432%
Toluene 108-88-3 18.99687 21.13855 -10.13163%
i
j
i .
56

COPY of RECORD Date Submitted: 6/27/2017 12:19:02
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:
1
i
l
r
i
57

SECTION 2
2016 SUPPORTING EMISSION CALCULATIONS
General Shale Brick, Inc. - Moncure, NC Facility I CY 2016 Emissions Inventory
Trinity Consultants

Title: 2016 Air Emission Inventory
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
Critical Parameters Table
Parameter I Value
Combustion Sources-Ca e Fear
Actual Brick Production U tons Per%car
Actual Sawdust Osage 0 t V
Combustion Sources-Brickhaven-, Yri 3 and Associated Drvers
Actual Brick Production(Natural Gas) 0 tPY
Actual Brick Production(Coal&NG) 0 tPy
Actual Gas Usage 0 scf/ r
Actual Coal Usage 0 tPy
Combustion Sources-Brickhaven-Kiln 4 and Associated Dn,ers
Actual Brick Production(Natural Gas) 118,725 tpy
Actual Brick Production(Coal&NG) 0 tPy
Actual Brick Production(Coal&NG) 0 Ib/hr
Acutal Gas Usage 261,729,307 scf/yr
Actual Coal Usage 0 tPY
Wood Waste System-Cape Fear
Number of Cyclones I1
Sawdust preparation I O hr/Vr
Clay Handling Operations
Actual Raw Material Processed 107,t46 tpy
Hours ofoperations 2.080 hr/yr
Intersite Conveyor
Process Throu,"h xA 107 tar, t»
Sand Dryer-Cape Tear
Hoursofo erations IL0;0 hr/Vr
Texturing Operations
Actual Brick Production 1 18,725 tpy
Ba house Efficiency 99.8%
Hours of operation-Brick Haven 2,800 hr/ r
Hours of operations-Cape Fear 0 hr/Vr
Vacuum Systems
Hours of o Aerations-Cape Fcar(VS I) 0 hr/Vr
Hours of operations-Brick Haven(VS2) 1,300 hr/ r
Hours of operations-Brick Haven(VS3)-Kiln 3 1,500 hr/ r
Lien. Bricl,Ha,e.,Wren n.VS5)
FI ash silo
HN ash silo IIIroughxu n
Cement Silo
Cement silo I hrough xn t x
Mixer Loading
Mixer Loading Throughput 0 t pV
Aggregate Loading "
Aggregate Loading"fhrough ut (! t V
Rumbler
I lours of o>erations hr'Vr
Fuel Usage
Dicsel l ank 66.221 gal/yr
Gasoline Tank 1,925 al/ r
Waste Oil Tank 750 al/ r
Motor Oil Tank 2,646 gaUyr
Brick Oil Tank 1292 al/ r
Gear Oil Tank 301 al/ r
Reference:
Information Provided by Warren Paschal,General Shale Brick,Inc.,June 6,2017
Support Calculations File: General Shale Moncure CY2016 El
Printed:6/27/2017 Page 1 of 35 Sheet: Input

Title: 2016 Air Emission Inventory _
Source ID N: ES-KI,ES-K2,ES-SDI
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID N - 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 AP-42 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.
Actual Brick Production 0 tpy
Actual Sawdust Usage - tpy
EMISSION CALCULATIONS
Emissions are calculated by the following equation:
Yearly Emissions
Emission Factor(lb/tons brick) Brick Production(tpy)=Emissions(lb/yr)
Emissions(lb/yr)/2000 lb/ton=Emissions(tpy)
Note:The Formaldehyde emissions are multiplied by the wood usage instead of bricks usage.
t
I
Support Calculations File:General Shale Moncure CY2016 El
Printed:6272017 Page 2 of 35 Sheet:Brick-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
ys�*�� ` �` �5 s � � Emisston Factor Ih%ton rinnualy �
r, s TAP NO CAS NQ ( EmlW, Rate 2 Emtss�on Rate
Nil
' � ) fi ed backs produced)
PM 0.675 Id 0 0.00
PM-10 0.675 Id 0 0.00
PM 2.5 0.675 0
S02 0 0.00
NOx 0.37 'd O 0.00
VOC 0.18 0 0.00
CO 0:344 d 0 0.00
1,4-dichlorobenzene 36 10646-7 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) 35 954&7 2.40E-09 ab 0.00E+00 0.00E+00
Acrylonitrile 4 107-13-1 1.90E-05 'b O.00E+00 O:00E+00
Antimony HAP ANTIMONYCPDS 2.80E-06 O.00E+00 0.00E+00
Arsenic 9 ARSEMCCPDS 2.10E-05 0.00E+00 0.00E+00
Benzene 12 1143-2 5.60E-04 a6 0.00E+00 0.00E+00
Beryllium 16 BERYLCPDS ' 3.10E-07 0.00E+00 0.00E+60
- 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 'b 0.00E+00 0.00E+00
Cadmium 23 CADMIUMCPDS 2.20E-05 0.00E+00 0.00E+00
Carbon Disulfide 27 75-15-0 1.80E-05 ab 0.00E+00 0.00E+00
Carbon tetrachloride 28 56-23-5 3.80E-07 °b 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 a6 0.00E+00 0.00E+00
I
Chloromethane(Methlyl Chloride) HAP 74-87-3 0.0014 a6 0.00E+00 O.00E+00
Chromium(expressed as*chromic
acid) HAP CROMCPDS 4.80E-05 0.00E+00 0.00E+00
Cobalt HAP 744048-4.. 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 a6 0.00E+00 0.00E+00
Di-n-butylphthalate HAP 84-74-2 1.60E-05 I''b 0.00E+00 0.00E+00
Ethylbenzene HAP 100414 1.00E-05 °b 0.00E+00 0.00E+00
Fluorine 50' 0.00E+00_ 0.00E+00
Formaldehyde 51 50-00-0 6.63E-03 0.00 0.00E+00
Hydrazine HAP - 0.00E+00 0.00E+00
Hydrogen Fluoride 59 7664-39-3 0.23 b 0.00E+00
HCl 57 7647-01-0 0.17 'r 0.00E+00
Hydrogen Sulfide 60 7783-064 j 0.00E+00 0.00E+00
lodomethane(Methyl Iodide) HAP 74-88-4 2.40E-04 b 0.00E+00 0.00E+00
Lead HAP LEADCPDS 1.20E-04 °' O.00E+00 0.00E+00
M-/p-Xylene HAP 108-38-3/10642-3 2.90E-05 1°b 0.00E+00 0.00E+00
Manganese 62 MANGCPDS 4.80E-04 1°' 0.00E+00 0.00E+00
III-Trichloroethane 1
(methylchloroform) 68 71-55-6 5.20E-07 °b 0.00E+00 0.00E+00
Methylene Chloride 69 74-87-3 6.20E-05 Jab 0.00E+00 0.00E+00
Mercury 66 NERCCPDS 1.10E-05 1" 0.00E+00 0.00E+00
Naphthalene HAP 91-20-3 2.40E-09 I'b 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 1°b 0.00E+00 0.00E+00
Ozone ; 0.00E+00 O.00E_+00
Perchloroethylene
(Tetrachloroethene) 81 127-184 3.80E-07 1'b 0.00E+00 0.00E+00
Phenol 82 108-95-2 1.00E-04 ia6 0.00E+00 0.00E+00
Phosphine 71 0.00E+00 0.00E+00
I
Support Calculations Fite'General Shale Moncure CY2016 El
Noted:6272017 page 3 of 35 Sheet Brick-CF(G-66) _

i
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 10042-5 4.20E-06 a6 0.00E+00 0.00E+00
Toluene 97 108-88-3 4.30E-04 a6 0.00E+00 0.00E+00
Total Fluorides(including HF) 50 1698448-8 0.27 b 0.00 0.00E+00
Trichlorofluoromethane 100 75-694 I.00E-06 ab O.00E+O 01 0.00E+00
Vinyl acetate HAP 108-054 1.90E-07 ab 0.00E+00 0.00E+00
Xylene 104 1330-20-7 3.63E-05 0.00E+00 I 0.00E+00
Emission factors from AP42,Section 11.3,8/97
a' Table 11.3-7 for sawdust fired kilns and sawdust dryer.
ab Table 11.3-6 for sawdust fired kilns and sawdust dryer.
ae Table 11.3-2 for sawdust fired kiln and sawdust dryer.
ad Table 11.3-3 for sawdust fired kilns.
Table 11.3-5 for sawdust fired kilns and sawdust dryer.
ar Table 11.34 for uncontrolled sawdust or natural gas fired tunnel kiln.
b Based on General Shale Brick Moncure Facility Stack Testing-DAQ requires TF=Fluorides of 0.04 lb/ton+HF of 0.23 lb/ton)
Emission factor provided by NCDENR,the emission factor basis is pound of emissions/tons of wood;
therefore,the factor is multiplied by the wood used.
Sawdust Usage from input Table= tpy
d Testing was perfonned on Kiln I and Kiln 2 in June 2006.Emission Factors are as follows:
Process weight rate during test for both kilns 22.3 ton/hr
Highest Emissions Rate Emission's
Pollutant is . Tesfed(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
I
wAighest Run EmissionsIpisslorl�
1 kollutant !-,. Rate Tested(Ib/h,i) 1"actor(IbJton)
S02 0.56 0.029
S02 factor for wood combustion AP42-Section 1.6 0.025 Ib/MMBtu
MMBtu for wood=Tons wood fired •2000 lb/ton•8000 Btu/lb
MMBtu for wood= 0 MMBtu
S02 Emissions=Tested lb/ton Actual Production ton/yr+ Wood Combustion Factor Ib/Mmbtu MMBtuyr fired
S02 Emissions= - lbs/yr -
l
Support calculations - File:General Shale Moncure CY2016 El
Printed:6272017 Page 4 of 35 Sheet:Brick-CF(G-66)

Title: 2016 Air Emission Inventory
Source 1D#: ES-K3K
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 Tonslyr
Coal Fired 0 Tonslyr
Brick Kiln Fuel: Coal[NG
60%Coal
40%Natural Gas
Control Eff.of HF 90% (NESHAP Requirement)
Uncontrolled � L'
Uncontrolled i h
TA orC
r,P NO F f f Ref Factor for Tested
acto oa 'N at ral Emi ? Total„,
u Gas sslon Annual Annu Pollutant
from AP 42=t $ r r
from AP 42 Ref Factors Ref Emisslons Emtsstons l
x Ib%ton (Iti/ttin) ,(Il hon) ;¢ (Ib/'r.)
PM 4.12E-01 0.00 0.00E+00
PM-10 2.03E-01 s 0.00 0.00E+00
PM-2.5 2.03E-01 s 0.00 0.00E+00
S02 38.000 f 2.86E-02 d 0.00 0.00E+00
NOx 8.13E-01 a 0.00 0.00E+00
VOC 2.40E-02 ad 2.40E-02 ad 0.00 0.00E+00
CO d, 8.00E-01 ab 0.83 ai 0.00 0.00E+00
Chlorine 29 1.30E-03 of 0.00 0.00E+00
HF 59 3.81E-01 d 0.00 0.00E+00
HCl 57 5.82E-02 d 0.000 0.00E+00
I I I-Trichloroethane 68 1.70E-05 ae 4.70E-06 of 0.00E+00 0.00E+00
(meth lchloroform)
Methylene Chloride 69 8.00E-07 ac 0.00E+00 0.00E+00
Perchloroethylene 81 2.80E-06 of 0.00E+00 0.00E+00
(Tetrachloroethene)
1,1-dichloroethane HAP 5.00E-06 9e 0.00E+00 0.00E+00
1,4-dichlorobenzene 36 3.20E-06 ae 4.80E-05. of 0.00E+00 0.00E+00
2-butanone(MEK) 70 2.50E-04 ae 2.20E-04 of O.b0E+00 0.00E+00
2-Hexanone NA 9.40E-07 ae 8.50E-05 of 0.00E+00 O-00E+00
2-methylphenol(cresol) 35 2.20E-06 ae 0.00E+00 0.00E+00
2-methylnaphthalene NA 1.70E-06 x 5.70E-05 of 0.00E+00 O.00E+00
Antimony NA 2.70E-05 ah 0.00E+00 0.00E+00
Acetone NA 6.80E-,04 ae 1.70E-03 of 0.00E+00 0.00E+00
Arsenic 9 1.30E-04 ag .3.10E-05 ah 0.00E+00 0.00E+00
Benzene 12 2.90E-04 ae 2.90E-03 ae 0.00E+00 0.00E+00
Benzoic Acid 2.50E-04 ae 0.00E+00 0.00E+00
Beryllium 16 1.60E-05 ag 4.20E-07 ah 0.00E+00 0.00E+00
Bis(2-ethylhexyl)phthalate;di(2- 39 7.30E-05 x 2.00E-03 of 0.00E+00 0.00E+00
eth lhex 1) hthalate
Bromomethane(Methyl Bromide) HAP 2.40E-05 ae 0.00E+00 0.00E+00
Butylbenzylphthalate NA 120E-06 ae 1.80E-OS af. 0.00E+00 0.00E+00
Cadmium 23 1.50E-05 ah 0.00E+00 0.00E+00
Support Calculations File: General Shale Moncure CY2016 El
Printed:612712017 Page 5 of 35 Sheet Brick-BH(ES-K3K G12)NG&Coal

Carbon Disulfide 27 230E-06 4.30E-05 of 0.00E+00 0.00E+00
Carbon tetrachloride 28 LOOE-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 ae 5.70E-04 of 0.00E+00 0.00E+00
Choroethane)
Chloroform 31 1.00E-07 ac 0.00E+00 0.00E+00
Chloromethane(Methyl Chloride) HAP 1.10E-04 90 6.70E-04 of 0.00E+00 0.00E+00
Soluble Chromate Compounds 5.10E-05 ah 0.00E+00 0.00E+00
Cobalt 2.10E-06 ah 0.00E+00 0.00E+00
Dibenzoftran NA 3.60E-07 a` 0.00E+00 .0.00E+00
Diethylphthalate HAP 1.40E-06 ac 2.40E-04 of 0.00E+00 0.00E+00
Dimethylphthalate HAP 7.80E-07 x 0.00E+00 0.00E+00
Di-n-butylphthalate HAP 1.40E-04 of 0.00E+00 0-00E+00
Di-n-octylphthalate 1.20E-05 ac 0.00E+00 0.00E+00
Ethylbenzene HAP 2.10E-05 ae 4.40E-05 of 0.00E+00 0.00E+00
Formaldehyde 51 7.50E-02 b 0.00E+00 0.00E+00
lodomethane(Methyl Iodide) HAP 930E-05 of 0.00E+00 0.00E+00
lsophorone HAP 3.00E-05 ae O.00E+00 0.00E+00
Lead NA 1.50E-04 ah 0.00E+00 0.00E+00
M-/p-Xylene HAP 130E-04 ae 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 ae 6.50E-05 ae 0.00E+00 0.00E+00
Nickel 75 7.20E-05 ah 0.00E+00 0.00E+00
o-Xylene HAP 4.70E-05 ae 5.80E-05 de 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 x 0.00E+00 0.00E+00
Phosphorus HAP 9.80E-04 ag 0.00E+00 0.00E+00
Selenium NA 2.30E-04 ah 0.00E+00 0.00E+00
Styrene 91 1.00E-07 ae 2.00E-05 ac 0.00E+00 0.00E+00
Toluene 97 2.50E-04 de 1.60E-04 ae 0.00E+00 0.00E+00
Total Fluorides 50 6.10E-01 0.00E+00 0.00E+00
Trichlorofluoromethane 100 1.40E-05 ae 0.00E+00 0.00E+00
Vinyl acetate HAP 1.00E-07 ae 0.00E+00 0.00E+00
'Emission factors from AP42,Section 11.3,8/97
as Table 11.3-1 for uncontrolled coal-fired and natural gas-fired kilns.
PM for condensible PM= 0.59 lb/ton
abTable 11.3=3 for coal-fired and natural gas-fired kilns.
"Table 11.34 for coal-fired and natural gas-fired kilns
A Table 11.3-5 for brick kilns.
'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
Soluble Chromate Compounds is the regulated NC TAP
b Emission factors from AP42,Section 1.4,7/98. The emissions factor in in Ib/mmft'of gas. The actual gas rate:
Formaldehyde Emission Factor=
0.0 MMBtu/hr/1020 Btu/ft'*10'Btu/MMBtu/10^(ft'/MMft')= 0.0000 mmft3/hr
` Using AP42 background information,assume that total fluorides emission factor is 60%of the HF emission factor
Also DAQ requires that total fluorides include HF,therefore TF=fluorides+HF(lb/yr)
TF=((0.381 Ib/ton'0.60)+0.381 lb/ton)'Brick Production ton/yr (1 -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 CY2016 El
Printed:6/27/2017 Page 6 of 35 Sheet: Brick-BH(ES-k3K G12)NG&Coal

y or
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
**S02 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
r AP-42 coal combustion _
Ap42 Emission Factor:Section 1.1 Table 1.1-3 38S lb/ton coal fired
Sulfur Content of Fuel 1.000% '
SO2 EF= 38 lb/ton coal fired
a 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:
e� V¢rage r x
Emrssions�j tes Emissron•actor
Pollutant Tested(lb/hr); (lblton)
PM 6.1 0.412
PM to 3 0.203
PM,., 3 0.203
I
Support Calculations File: General Shale Moncure CY2016.El
Printed:6/27/2017 Page 7 of 35 Sheet: Brick-BH(ES-K3K_G12)NG&Coal

Title: 2016 Air Emission Inventory
Source ID ES-K3D1,ES-K3D2,ES-K3D3
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID M 1900009
Source: ES-K3D1,ES-K3D2,ES-K3D3 Brick Dryers 1,2,and 3 on Kiln 3
Actual Production: Tons/yr
Brick Dryer Fuel: NG/Propane
Em>tss�on Factors �Efnissiow, a e
Poll t
PM 0.187 Iac 0.00 0.00
PM-10 0.187 Jac 0.00 0.00
PM-2.5 0.187 Jac 0.00 0.00
--T
SO2 0.00
NOx 0.098 as 0.00 0.00
VOC 0.03 * jab- 0.00 0.00
CO 0.31 as 0.00 0.00
Fon-naldehyde 1.55 -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 Mdncure CY2016 El
Printed:6/27/2017
Page 8 of 35 Sheet: Brick-BH(ES-K3K—G1 2)(total)

I
Title: 2016 Air Emission Inventory
Source ID#: ES-K4K
j Facility: General Shale Brick,Inc
Location: Moncure,NC
Facility ID#: 1900009
Brick Processing System-Brick Haven-Kiln 4
r
d
Source: ES-K4K Kiln 4
Actual Brick Production: 118,725 Tonslyr
Coal Fired 0 Tons/yr
Brick Kiln Fuel: Coal/NG
Percentages if Coal Fired: 60%Coal
40%Natural Gas
Control Eff.of HF 90% (NESHAP Requirement)
-� IN CY 2016,Fired NCY Only
� ",-,Rnitssionvl
TAP NO. Faec for' Tested
Natural as.- Em►sston Annual Total Annual `
Pollutant from AP 42 Ref•Factors Red Emtsstons Emtsslons:
y (Ib/ton)
PM 1.04E-01 w e,as 82,377 41.19
{ PM-10 1.04E-01 e,aa 82,377 41.19
1 PM-2.5 1.04E-01 e,as 82,377 41.19
S02 2.86E-02 d 1,358 0.68
NOx 3.50E-01 ab 41,554 20.78
1 VOC 2.40E-02 ad 2,849 1.42
CO 0.83 ai 98,542 49.27
1 Chlorine 29 1.30E-03 of 154, 0.077
! HF 59 5.77E-03 a 685.0 3.42E-01
HCl 57 2-63E-02 e 3,120 1-56E+00
III-Trichloroethane 68 4.70E-06 of 5.58E-01 2.79E-04
(methylchloroform)
Methylene Chloride 69 0.00E+00 0.00E+00
Perchloroethylene 81 2.80E-06 of 3.32E-01 1.66E-04
(Tetrachloroethene)
1,1-dichloroethane HAP 0.00E+00 0.00E+00
1,4-dichlorobenzene 36 4.80E-05 of 5.70E+00 2.85E-03
2-butanone(MEK) 70 2.20E-04 ar 2-61E+01 1.31E-02
2-Hexanone NA 8.50E-05 ar 1.01E+01 5.05E-03
2-methylphenol(cresol) 35 0.00E+00 0.00E+00
2-methylnaphthalene NA 5.70E-05 of 6.77E+00 3.38E-03
Antimony NA 2.70E-05 A 3.21 E+00 1.60E-03
Acetone NA 1.70E-03 of 2.02E+02 1.01E-01
4 Arsenic 9 3.10E-05 ah 3.68E+00 1.84E-03
_ Benzene 12 2.90E-03 3.44E+02 1.72E-01
Benzoic Acid 0.00E+00 0.00E+00
Beryllium 16 4.20E-07 ah 4.99E-02 2.49E-05
Support Calculations File: General Shale Moncure CY2016 El
Printed:6127/2017 Page 9 of 35 Sheet: Brick-BH(ES-K4K_G12)NG&Coal

Bis(2-ethylhexyl)phthalate; 39 2.00E-03 of 2.37E+02 1.19E-01
di(2-ethylhexyl)phthalate
i Bromomethane(Methyl HAP 0.00E+00 0.00E+00
Bromide)
k
4
. I
i
Support calculations file: General Shale Moncure CY2016 El
Printed:6/27/2017 Page 10 of 35 Sheet: Brick-BH(ES-K4K G12)NG&Coal

Butylbenzylphthalate NA 1.80E-05 of 2.14E+00 1.07E-03
Cadmium 23 1.50E-05 ah 1.78E+00 8.90E-04
Carbon Disulfide 27 4.30E-05 of 5.11E+00 2.55E-03
Carbon tetrachloride 28 0.00E+00 0.00E+00
Chlorobenzene HAP 0.00E+00 0.00E+00
Chloroethane(Ethyl HAP 5.70E-04 of 6.77E+01 3.38E-02
Chloride)
Chloroform 31 0.00E+00 0.00E+00
Chloromethane(Methyl HAP 6.70E-04 of 7.95E+01 3.98E-02
Chloride)
_ Soluble Chromate 5.10E-05 ah 6.05E+00 3.03E-03
Compounds
Cobalt 2.10E-06 ah 2.49E-01 1.25E-04
Dibenzofuran NA 0.00E+00 0.00E+00
Diethylphthalate HAP 2.40E-04 of 2.85E+01 1.42E-02
Dimethylphthalate HAP 0.00E+00 0.00E+00
Di-n-butylphthalate HAP 1.40E-04 of 1.66E+01 8.31 E-03
Di-n-octylphthalate 0.00E+00 0.00E+00
Ethylbenzene HAP 4.40E-05 of 5.22E+00 2.61 E-03
Formaldehyde 51 7.50E-02 b 1.96E+01 9.81E-03
lodomethane(Methyl HAP 9.30E-05 of 1.10E+01 5.52E-03
Iodide)
Isophorone HAP 0.00E+00 0.00E+00
Lead NA 1.50E-04 ah 1.78E+01 8.90E-03
M-/p-Xylene HAP 6.70E-05 of 7.95E+00 3.98E-03
Manganese 62 2.90E-04 ah 3.44E+01 1.72E-02
Mercury 66 7.50E-06 ah 8.90E-01 4.45E-04
j Naphthalene HAP 6.50E-05 ac 7.72E+00 3.86E-03
i
Nickel 75 7.20E-05 ah 8.55E+00 4.27E-03
o-Xylene HAP 5.80E-05 ac 6.89E+00 3.44E-03
Perchloroethylene of 3.32E-01 1.66E-04
(Tetrachloroethene) 81 2.80E-06
Phenol 82 8.60E-05 de 1.02E+01 5.11 E-03
Phosphorus HAP 0.00E+00 0.00E+00
Selenium NA 2.30E-04 ah 2.73E+01 1.37E-02
Styrene 91 2.00E-05 ac 2.37E+00 1.19E-03
Toluene 97 1.60E-04 ac 1.90E+0] 9.50E-03
Total Fluorides 50 9.23E-03 c 1,096 5.48E-01
Trichlorofluoromethane 100 0.00E+00 0.00E+00
I
Vinyl acetate HAP 0.00E+00 0.00E+00
'Emission factors from AP42,Section 11.3,8/97
"Table 1 1.3-1 for uncontrolled coal-fired and natural gas-fired kilns.
i PM for condensible PM= 0.59 lb/ton
abTable 11.3-3 for coal-fired and natural gas-fired kilns.
"Table 11.3-4 for coal-fired and natural gas-fired kilns
! ad Table 11.3-5 for brick kilns.
f 'rTable 11.3-6 for natural gas-fired kilns
A Table 11.3-7 for natural gas-fired kilns.
ai Factor is from AP42 Background Document testing at
Marseilles Brick which has the same type of kiln
a/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;of gas. The actual gas rate:
' Actual Gas Usage- 261,729,307 scf/yr = 261.73 mmft3/yr
Support Calculations File: General Shale Moncure CY2016 El
Printed:6/27/2017 Page 11 of 35 Sheet: Brick-BH(ES-K4K G12)NG&Coal

1
` Using AP-42 background information,assume that total fluorides emission factor is 60%of the HF emission factor
_ I 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
£r r r€s Y r Em-[ssIOrIS Rate Emission Factor
Pollutant '§ ,. Tested(Ib%fir) - --,(Ib/tou),,,;:. •
I 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
`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:
` �' Emissions Rate Emission Factor
Pollutant _' .Tested.(Ibhc}„ -;,(Ib/ton)' ;:
PM 1.6 0.10
HCI 0.41 2.628E-02
HF 0.09 5.769E-03
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Support Calculations File:General Shale Moncure CY2016 El
Printed:6/2712017 Page 12 of 35 Sheet: Brick-BH(ES-K4K_G12)NG&Coal

Title: 2016 Air Emission Inventory
Source ID#: ES-K4D1,ES-K4D2,ES-K4133
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: 118,725 Tons/yr
Brick Dryer Fuel- NG/Propane
xaFF� 7 s x S rVr r; 1 a t B A7lnual E�nnual
r' ,, 3 Em�ss>on Factor�(Ib/ton fired Em>fss>ton Rate Eru ssibn
Pollutant s r b'r�cks roduced lb! r Rate TPY
m. ) Y ) �•
PM 0.187 ad 22 202 11.10
]'
PM-10 0.187 lad 22,202 11.10
PM-2.5 0.187 ad 22,202 11.10
SO2
NOx 0.098 as 11,635 5.82
VOC 0.03 lab 3,562 1.78
CO 0.31 ac 36,805 18.40
Formaldehyde 1.55E-01 b
t a Emission factors from AP-42, Section 113, 8/97
as Table 11.3-3 for brick dryer with supplemental gas burner
ab Table 113-5 for brick dryer.
ac Table 113-5 for brick dryer.
ad Table 11.3-1 for brick dryer.
b The formaldehyde emissions from the dryer are included in the kiln calculation.
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Support Calculations File: General Shale Moncure CY2016 El
Printed:6/27/2017 Page 13 of 35 Sheet: Brick-BH(ES-K4K_G12)(total)

Till 2016 Air Emission Inventory
Source ID 0: ES-K],ES-K2,ES-SDI,ES-K2K ES-K41(,ES-K4D1,ES-K4D2,ES-K4D3
Facility:
General Shale Brick,Inc.
Location: Mo.curc,NC
Facility ID 1900009
Q4
V, X,
51'i �Kiln 3Kiln�-Kiln aven 3 ,Kfln ji ��' 4 Kil." Kiln,4 v Briekha en 4 Total `
1py.,,�. o 9 yr Drycir(ipj), Total(11h6r) TPY
tall(tori<yr) ;,To
PM 0.00E+00 0.00E+00 0.00E+00 4.12E+01 1.11 E4101 52,29 1.05E405 52.29
PM-10 0.0011+00 0.00E+00 0.00E+00 4.12E+01 1.11E+01 52.29 1.05E+05 52.29
PM 2.5 0.00E400 0.00E+00 0.00E+00 4.12E+01 1.11 E+01 52.29 1.05E+05 52.29
S02 0.00E+00 0.00E+00 0.00E+00 6.79E-0 I 0.00E+00 0.68 1.36E+03 0.68
NO. 0.00E+00 0.00E400 2.08EQI 5.82E+00 26.59 5.32E+04 26.59
VOC 0.0 0.00E+00 1.42E+00 1.78E00 321 641 E+03 3-21
O.00E+00 024 E+01
Co WE O.00E+00 4.93E+01 1.84 67.67 67.67
Minds7yr,
Woad Kilos&
Bnckbaveri3 7 Kln 4IGI. 4 Brickh­�.4. �,Totil­.-
:� "Dryer
i 1
"J* blyF) Tp
iyr) Totol.ptilyr) Total(I.�b
10646-7 0.00E+00 O.00E40 0 1,4-dichlomben- 0.00E+00 5.70E+00 5.70E+011 5.7UE4*0 2.85E-03
2-b.taw.(MEK) 70 78-93-3 0.0013+00 0.00E+00 0.00E4*0 2.61 E+O 1 2.61 E+O I 2.61E+01 1.31 E-02
2-methviphmol(cresol) 35 9548-7 0.00E+00 0.00E400 0.00E+00 0.00E4100 OaOOE+W 0a00E+00 O.00E+OU
Acrylonitrile 4 107-13-1 0.00E+00 0.00E400 0.00E4100 0,00E400 0.00E+00 O.00E+00 O+OOEQO
Antimony HAP ANTIMONYCPDS O.00EQO 0.00E+00 0.00E+00 3.2 1 E4 00 3.2 1 EQU 3.21E+00 1.60E-03
Arsenic 9 ARSENICCPDS 0.00E+00 0.00E+00 0+00E+00 3.68E400 3'68E+00 3.68E+00 1.84E-03
Bc.u- 12 7143-2 0.00E+00 0.00E+00 D.00E+00 3+44E+02 3.44E+02 3.44E+02 1.72E-01
Beryllium 16 BERYLCPDS 0.00E+00 0.00E+00 0.00E41D0 4.99E-02 4.99E-02 499E-02 2.49E-05
Bis(2­cthylhexyl)phthalatc;di(2- 117-87-7 O.00E+00 9 1
cthylhcxyl)phthalate 39 O.OGE41DO O.00EQO 2+37E+02 2.37E-R)2 2.37F+02 1.19E-01
Bromomethane(McIW,Bromide) HAP 74-83-9 0.00E+00 0.00E40D 0.00E+00 0.00E+00 O.00E+00 0w00E+W O.00E400
Cadmium 23 CADMILJMCPDS 0.00E+00 0.00E4100 0.00E+00 1.78E+00 1.78E+00 1.78E41DO 8.90E-04
Carbon Disulfide 27 75-15-0 0.00E+00 0.00E+00 0.00E+00 5.11 E400 5.11 E40U 5.11 E+00 N2+55E-03
Carbon ictrachloridc 28 56-23-5 0-00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 O.GOE+M 0.00E400
Chlorine 29 0.00E+00 0.00E+00 O.00E+00 1.54E+02 1.54E+02 1.54E+02 7.72E-02
Chlorocth...(Ethyl Ch-th-) HAP 75-00-3 0.00E400 0.00E+00 0.00E+00 6.77E401 6.77E+01 6.77E+0 I 3.38E-02
Chloroform 31 67-66-3 0.00E+00 0.00E+00 0.00E400 O.00E+W 0.90E400 O.OUE+00 0.00E400
Chl-thane,(Methly Chloride) HAP 74-87-3 0.00E400 0.00E+00 0.00E+00 7.95E+01 7.95E+01 7.95E40I 3.98E-02
Chromiuni(expressed as chromic 'id) HAP CROMCPDS 0.00E+00 0.00E+00 0.00E+00 6.05E+00 6.05E+00 6.05E+00 3.03E-03
Cobalt HAP 7440484 0.0011+00 O.00E+00 0.00E+00 2*49EwOl 2.49E-01 249E-01 1.25E-04
Dicthylphtlialate HAP 84-66-2 0.0013+00 0.00E+00 0.00E+00 2.85E+01 2.85E+01 2.85E+01 1.42E-02
Di-thylphthalate HAP 131-11-3 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.(YOE+(10 01I0E400 0.00E+00
DFn-butylphilialate HAP 84-74-2 0.00E+00 0.00E+00 0.00E+00 1.66E+01 1.66E+01 1d66E+01 8.31 E-03
Ethylb- HAP 100-41-4 0.00E+00 0.00E+00 0.00E+00 5.22E+00_ 5.22E+00 5.22E+00 2,61 E-03
Fluorine 50 0.00E+00 0.0011+00 0.00E+00 0.00E+00 0.00E+00 tME+0 O.00E+00
Fo-Whyd. 51 50-00-0 0.00E+00 0.00E+00 0.00F+00 1.96E+01 1.96E+01 1.96E+01 9.8113-03
Hydrazine HAP O.00E+OD 0.00E+00_ 0.00E4100 0.00E+00 0.00E+00 0.00E+00 0.00E+00
HF 59 7664-39-3 0.00E+00 0.0011+00 0.00E+00 6.85E+02 6.85E+02 6.85E+02 3.42E-01
HCI 57 7647-01-0 0.00E+00 0.00E+00 0.00E+00 3.12E+03 3.12E+03 3.12E+03 1.56E+00
Hydrogen Sulfidc 60 7783-06-4 0.00E+00 0.00E+00_ 0.00E+00 0.0013+00 0.00E+00 0.00E+00 0.00E+00
lodonicthano(Mctkvl Iodide)_ HAP 74-884 0.00E+00 0.00E+00 0.00E+00 1.10E+01 LJUE+01 1.10E+01 5.52E-03
Lead HAP LEADCPDS 0.0011+00 0.00E+00 O.00E+00 1.78E+01 1.78E+01 179E+01 8.90E-03
m4p-x)[me HAP 108-38-3/10642-3 0.00E+00 O.00E+00 0.00E+00 7.95E+00 7.95E+00 7.95E+00 3.98E-03
Manganese 62 MANGCPDS 0.00E+00 O.00E+00 0.00E+00 3.44E+01 3.44E+01 3.44E+01 1.72E-02
I I I-Trichlorwhane 69 71-55-6 0.00E+00(
Mik0chl.roform) O.00E+00 O.00E+00 5.58E-01 5.58E-01 5.58E-01 2.79E-04
Methylene Chlodd. 69 74-97-3 0.00E+00 O.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00
M-- 66 MERCCPDS 0.00E+00 0.00E+00 0.00E+00 8.90E-01 8.90E-01 8.90E-01 4.45E.04
Naphthalene HAP 91-20-3 OME+00 0.00E+00 0.0011+00 7.72E+00 7.72E+00_ 7.72E+00 3.86E.(13
Nickel 75- NICKCPDS 11.00E+00 0.00F+00 0.00E+00 8.55E+00 8.55E+00 8.55E4410 4.27E-03_
c­xYlme HAP 9547-6 0.00E+00 0.00E+00 O.00E+00 6.89E+00 6.89E+00 6.89E+00 3.44E-03
Ozone 0.00E+00 0.00E+00 0.00E+00 0.00E+00_ 0.(I0E+(1() Om00E+00 0.00 +00
P-bloroethy1mc(Tetrachloroefficne) 81 127-184 0.00E+00 0.00E+00 0.00E+60 3.32E-01 3.32E-01 3.32E-01 1.66E-04
Phenol 82 108-95-2 0.00E+00 O.00E+00 0.00E+00 1.02E+01 1.02E+01 1.02E+01 5.11 E-03
Phos,phine 71 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00
Phosphorus HAP 7723-14-0 0.00E+00 0.0011+00 O.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00
Selenium HAP SEC 0.00E+00 0.00E+00 0.00E+00 173E+01 2.73E+01 2.73E+01 1.37E-02
St)-. 91 10042-5 O.00E+00 O.00E+00 O.00E+00 2.37E+(10 2.37E+00 2.37E+00 1.19E-03
Macao 97 108-88-3 0.00E+100 0.00E+00 0.00E+00 1.90E+01-,- 1.90E+01 1.90E+0 I 9.50E-03
Total Fluorides(including HF) 50 1699448-8 O.00E+00 ��.602EM IFO r 1!512� 3 I.IOE+03 1.10E+03 5.48E-01
75-694 0.00E+00 +,)o 0.00E+00 O.00E+00 O.00E+00
Yn Womfluoromthane 100
Vinyl acclatc, HAP 108-054 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00 0.00E+00 iE: E
'2 0
+0,
Xylenc 104 1330-20-7 0.00E+00 0.00E+00 O.00E+00 IASE+01 1.48E.. M402 13
SupportCakd R b- .:General ShW.MarcusCY2016 El
PM.6272917 Rap 14 of 35 Sheet Bnck-Sum

Title: 2016 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 2016
An' dA
V
Emission Factor Em><ss><bn
Pollutant -,
Rate W a
PM 1.10 0.00E+00 0.00E+00
PM-10 1.10 0.00E+00 0.00E+00
PM-2.5 1.10 0.00E+00 0.00E+00
Emission factors from AP-42, Section 12.2, Coke Production, Table 12.2-2, 8/97
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
Support Calculations File: General Shale Moncure CY2016 El
Printed:6/27/2017 Page 15 of 35 Sheet: ES-Coal Crusher

Title: 2016 Air Emission Inventory
Source ID#: ES-WFS
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
I
Wood Fuel/Sawdust System
i
Source: ES-WFS Wood Fuel/Sawdust System
Hours of Operation 0 hrs
Wood Fuel/Sawdust System
Control: CD-SD-DCI Dust Collector
Description: Two conveyors,which feed materials to the two screens,are both controlled by a dust collector.
I
EPN: EP-SD-DC1 Did Not Operate in 2016
Source: ES-SD-SC1 8x8 Screen
ES-SD-SC2 8x8 Screen
ES-SD-CV1 Transfer Screw Conveyor
ES-SD-CV2 Screen Feed Screw Conveyor
Variables: Hours of Operation
Factors:
Exit Concentration= 0.01 gr/dscf
Flow Rate for System= 2100 cfm
Bagfflter Efficiency= 99%
Emissions Before Control
PM Emissions=Emissions After Control/(l -Efficiency)
PM Emissions= 18.0 lb/hr
Emissions After Control
PM Emissions=Exit Concentration* 1 lb/7,000 gr*Flow Rate*60 min/hr
R1VI Emiss>ons .i;0180' -. lb/tr
0; Ib/ r
Support Calculations File: General Shale Moncure CY2016 El
Printed:6/27/2017 Page 16 of 35 Sheet: Controlled New WFS(G-21)

Wood Fuel/Sawdust System
Controls: CD-SD-DC2 Dust Collector(2300 cfm)
i
Description: Dust collector is used for the PM exhaust from the hammermill and cyclone.
EPN: EP-SD-DC2
Did Not Operate in 2016
Source: ES-SD-CYC Cyclone
ES-SD-HM Hammermill
Variables: Hours of Operation
Factors:
t
Exit Concentration= 0.01 gr/dscf
Flow Rate for System= 2345 cfin
Bagfilter Efficiency= 99%
Emissions Before Control
PM Emissions=Emissions After Control/(1 -Efficiency)
PM Emissions= 20.1 lb/hr
Emissions After Control
PM Emissions=Exit Concentration* 1 lb/7,000 gr*Flow Rate*60 min/hr
P-M Emiss>ons " 0 201 1bXh"r
0, 1b7yr
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Support Calculations File: General Shale Moncure CY2016 El
Printed:6/27/2017 Page 17 of 35 Sheet:Controlled New WFS(G-21)

Wood Fuel/Sawdust System
Controls: CD-SD-BVI Bin Vent Filter
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Description: Storage silo,which is connected to a bin vent filter,is used as storage for the product.
EPN: EP-SD-BVI
Did Not Operate in 2016
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%
Emissions Before Control
PM Emissions=Emissions After Control/(1 -Efficiency)
PM Emissions= 3.4 lb/hr
J
Emissions After Control
PM Emissions=Exit Concentration* 1 lb/7,000 gr*Flow Rate*60 min/hr
PM Emissions= '� � 40 034 ,lb/hr
0 0 Ib/y`r
Support Calculations File: General Shale Moncure CY2016 El
Printed:6127/2017 Page 18 of 35 Sheet: Controlled New WFS(G721)

Wood Fuel/Sawdust System
Controls: CD-SD-BV2 Bin Vent Filter
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 2016
Source: ES-SD-SH Surge Hopper
Factors:.
Exit Concentration= 0.01 gr/dscf
_ Flow Rate for System= 400 cfin
Bagfilter Efficiency= 99%
Emissions Before Control
PM Emissions=Emissions After Control/(1 -Efficiency)
PM Emissions= 3.4 Ib/hr
Emissions After Control
V
_ - PM Emissions=Exit Concentration* I lb/7,000 gr*Flow Rate*60 min/hr
PM Fmisstons- ' �0 034,`� Itim'i ''
Total WFS Emissions
WFS Total
_ Pollutant (controlled) 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
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Support Calculations File: General Shale Moncure CY2016 El
Printed:6/27/2017 Page 19 of 35 Sheet: Controlled New WFS(G-21)

- . Title: 2016 Air Emission Inventory
Source ID#: Clay Handling
Facility: General Shale Brick,Inc.
Location: Moncure,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
Factors for-Grinding&Screening:
AP-42 Section 11.3,Table 11.3-2
Emission Factor for Grinding and Screening
PM emission factor 0.0250 lb/ton
PM-10 emission factor 0.0023 lb/ton
PM-2.5 emission factor 0.0023 lb/ton
Maximum Process Throughput 200 tph
Actual Raw Material Processed 107,146 tpy
Maximum Hours of Operation 2,080 hrs/yr
Control Efficiency for PM 0 % No Control Devices
Descnpt n,
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-FS 1 -F-FS9 One bank of nine finishing
screens(clay handling equipment
200 tph)
F-FC4 Finishing Conveyor 94(clay
handling equipment 200 tph)
NSPS
F-FC5 Finishing Conveyor#5(clay
handling equipment 200 tph)
NSPS
Pollutant Actual.Emtssaons,
Y tons% r
PM 2,678:65 1.34
PM-10 246 0.12
PM-2.5 246 0.12
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Support Calculations File: General Shale Moncure CY2016 El
Printed:6/27/2017 Page 20 of 35 Sheet: Clay Handling(G-71)

_ Title: 2016 Air Emission Inventory
Source ID#: Clay Handling
^� Facility: General Shale Brick,Inc.
Location: Moncure,NC
-- Facility ID#: 1900009
Source: ES-CH Clay Handling Equipment
SAMPLE CALCULATIONS
- Grinding&Screening Emissions
PM Actual Emissions(lbs/yr)
i 0.025 lb/ton * 107146 tpy = 2678.65 lbs/yr
PM Actual Emissions(tons/yr)
2678.65 lbs/yr/2000lb/ton = 1.34 tpy
PM-10 Actual Emissions(lbs/hr)
0.0023 lb/ton * 107146 tpy = 246.436 Ibs/yr
i -
PM-10 Actual Emissions(tons/yr)
246.4358 lbs/yr/2000lb/ton = 0.12 tpy
f
PM-2.5 Actual Emissions(lbs/hr)
0.0023 lb/ton * 107146 tpy = 246.436 lbs/yr
PM-2.5 Actual Emissions(tons/yr)
246.4358 Ibs/yr/2000Ib/ton = 0.12 tpy
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Support Calculations File: General Shale Moncure CY2016 El
Printed:6/27/2017 Page 21 of 35 Sheet: Clay Handling(G71)

2016 Air Emission Inventory General Shale Brick Inc.
Source: Intersite Conveyor Moncure Plant
Source: Conveyor from Cape Fear Plant to
Brickhaven Plant F-C-CFBH
Description: The calculations below quantify emissions from the new inter-site conveyor,which will be installed to
transport material from the reclaim building at the Cape Fear site to the ground storage building at
the Brickhaven site.
EPN: Fugitive
Controls: NA
Factors for Drop Points
Equations obtained from page 13.2.4-3 of AP-42
E=k(0.0032)[(U/5)^1.3/(M/2)^1.4](I-controleff/100)lb/ton
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)^1.4]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 mph/5)^1.3/(10/2)^1.41= 4.91E-04 lb/ton
PM<=2.5 microns:
0.053 *0.0032*[(15 mph/5)^1.3/(10/2)111.4]= 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.
f
Emissions estimated using the Drop Equations from AP42
,` Locaf�on x a ;%Throughpaf Drops
t ID Descnption It )
From Cape Fear to
Brickhaven ES-C Conveyor 107,146 1
Pollutant- g potential Emtsstons(per emtsston source)
Name '` (IbsJyr), � (tons/yr)
PM 111.19 0.06
PM-10 52,59 0.03
PM-2.5 7.96 0.00
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 CY2016 El
Printed:6/27/2017 Page 22 of 35 Sheet: IntersiteConv(Clay Handling)

SAMPLE CALCULATIONS
Grinding&Screening Emissions
PM Potential Emissions(Ibs/yr)
0.001 lb/ton* 107146 tpy* 1 drop= 111.19 Ibs/hr
PM Potential Emissions(tons/yr)
111 /2000lb/ton = 0.06 tons/yr
TOTAL EMISSION CALCULATIONS FOR CLAY HANDLING
Pollutant ar p` }' Potential Emrss�ons(per emrsston.source)
Namerr a :(Ibs/Yr)... (tons/yr)
PM 2789.84 1.39
PM 10 299.02 0.15
PM2.5 254.40 0.13
I _
Support Calculations file: General Shale Moncure CY2016 El
Printed:6/27/2017 Page 23 of 35 Sheet: IntersiteConv(Clay Handling)

Title: 2016 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#: VM0009
_ Texturing Operations
Sand Blasting Cabinets
Actual Brick Production-CIF 0 tons/yr
Actual Brick Production-BH 1]9,725 tons/yr
Hrs of Operation-Brick Haven 2800 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 1 l 8725 tpy
Scale Up Factor Potentials 1
Two Texturing Operations
Controlled by CD-CR6BF, CD-CR7BF,CD-CR7.BF2 and CD-CR7BF3
EMISSION CALCULATIONS
Brick Haven Brick Haven Cape Fear, Total
Pollutant Actual JEm>tss>tons„ Actual:>Emissions" A Actual Em ss><ons.
w 5
Name 16s/;r) _(tons/, r, (lbs/ r),,r (tons% -tons/,,r)
PM 427.41 0.214 0:00 0.000 427.41 0.214
PM-10 427.41 0.214 0.00 0.000 427.41 0.214
1 PM-2.5 427.41 0.214. 0.00 0.000 427.41 0.214
Support Calculations File: General Shale Moncure CY2016 El
Printed:6/27/2017 Page 24 of 35 Sheet: Text(G-69)

Title: 2016 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-CD813F
Variables: Hours of Operation
Dryer Fuel: Natural Gas with Propane/Air Standby
Dryer Gas Rate(MMBtu/hr)= 0.25 MMBtu/hr
Hours of Operation= 1,040 hrs
Bagfilter Control Efficiency= 99.9%
Heating Value for Natural Gas= 1020 Btu/ft3
Gas Usage(Calculated 3
based upon hours of operation)= 2.55E-01 mmft /yr
ncontrolled Em>Iss>lon actor Emissions EmISS10IlS.-
Pollutant Ref, e''(lb/yr) a(tPy)
b/mmft3) Rat Rat
P 3
M~ 0.52 6.04E+01 3.02E-02
PM-10 0.52 3 6.04E+01 3.02E-02
PM-2.5 0.52 3 6.04E+01 .02E-02
SO2 6.00E-01 ' 1.53E-01 7.65E-05
NOx 100 ' 2.55E+01 1.27E-02
VOCS 5.5 ' 1.40E+00 7.01E-04
CO 84 ' 2.14E+01 1.07E-02
2-Methylnaphthalene 2.40E-05 ' 6.12E-06 3.06E-09
3-Methylchloranthrene 1.80E-06 ' 4.59E-07 2.29E-10
7,12-Dimethylbenz(a)anathracene 1.60E-05 ' 4.08E-06 2.04E-09.
Acenaphthene 1.80E-06 ' 4.59E-07 2.29E-10
Acenaphtylene 1.80E-06 ' 4.59E-07 2.29E-10
Acetaldehyde 1.52E-05 2 3.87E-06 1.94E-09
Acrolein 1.80E-05 2 4.59E-06 2.29E-09
Anthracene 2.40E-06 ' 6.12E-07 3.06E-10
Ammonia 3.20E+00 2 8.16E-01 4.08E-04
Benz(a)anthracene 1.80E-06 t 4.59E-07 2.29E-10
Benzene 2.10E-03 ' 5.35E-04 2.68E-07
Support Calculations File: General Shale Moncure CY2016 El
Printed:6/27/2017 Page 25 of 35 Sheet: Dryer(ES-CD-8)

Benzo(a)pyrene 1.20E-06 I 3.06E-07 1.53E-10
Benzo(b)fluoranthene 1.80E-06 I 4.59E-07 2.29E-10
Benzo(g,h,I)perylene 1.20E-06 1 3.06E-07 1.53E-10
Benzo(k)fluoranthene 1.80E-06 I 4.59E-07 2.29E-10
Butane 2.1 5.35E-01 2.68E-04
Chrysene 1.80E-06 1 4.59E-07 2.29E-10
Dibenzo(a,h)anthracene 1.20E-06 1 3.06E-07 1.53E-10
Dichlorobenzene 1.20E-03 1 3.06E-04 1.53E-07
Ethane 3.1 1 7.90E-01 3.95E-04
Fluoranthene 3.00E-06 1 7.65E-07 3.82E-10
Fluorene 2.80E-06 I 7.14E-07. 3.57E-10
Formaldehyde 7.50E-02 I 1.91 E-02 9.56E-06
Hexane 1.8 1 4.59E-01 2.29E-04
Indeno(1,2,3-cd)pyrene 1.80E-06 I 4.59E-07 2.29E-10
Naphthalene 6.10E-04 I 1.55E-04 7.77E-08
Pentane 2.6 1 6.63E-01 3.31E-04
Phenanathrene 1.70E-05 1 4.33E-06 2.17E-09
Propane 1.6 1 4.08E-01 2.04E-04
Pyrene 5.00E-06 1 1.27E-06 6.37E-10
Toluene 3.40E-03 1 8.67E-04 4.33E-07
Arsenic 0.00E+00 . 2 0.00E+00 0.00E+00
Barium 4.40E-03 1 1.12E-03 5.61E-07
Beryllium 0.00E+00 2 0.00E+00 0.00E+00
Cadmium 0.00E+00 2 0.00E+00 0.00E+00
Chromium(as chromic acid) 0.00E+00 2 0.00E+00 0.00E+00
Cobalt 8.40E-05 I 2.14E-05 1.07E-08
Copper 8.50E-04 I 2.17E-04 1.08E-07
CO2 1.20E+05 2 3.06E+04 1.53E+01
Lead 5.00E-04 I 1.27E-04 6.37E-08
Manganese 0.00E+00 2 0.00E+00 0.00E+00
Mercury 0.00E+00 2 0.00E+00 0.00E+00
Methane 2.30E+00 I 5.86E-01 2.93E-04
Molybdenum 1.10E-03 I 2.80E-04 1.40E-07
N2O 2.20E+00 t 5.61 E-01 2.80E-04
Nickel 0.00E+00 2 0.00E+00 0.00E+00
Selenium 2.40E-05 I 6.12E-06 3.06E-09
Vanadium 2.30E-03 I 5.86E-04 2.93E-07
Zinc 2.90E-02 I 7.39E-03 3.70E-06
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
3 PM&PM-10 Emissions were calculated by adding natural gas combustion factors and(NC Spreadsheets
for PM,PM-10 from NEl)and factors for industrial sand dryers(AP-42,Section 11.19)
Support Calculations File: General Shale Moncure CY2016 El
Printed:6/27/2017 Page 26 of 35 Sheet: Dryer(ES-CD-8)

<>Parameter s . sr �:i+'t� y: a `TalUe ASS '
try i Yk
. . ..:. .
I
Maximum Hourly Coatings Rate 3.45 ton/hr
Maximum Annual Coatings Rate 30,222.00 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
i
PM/PM=10/PM-2.5 Emissions= 30222 ton/yr*2 lb/ton -
PM/PM-10/PM-2.5 Emissions= 60,444 lb/yr
Controlled Emissions= - 60 lb/yr
* Due to the lack of emission factors for this type of operation,the industrial sand
dryer emission factor from AP42,Section 11.19 was selected for use. It is felt that
this is a conservative factor because the factor is for mined quartzite that is
processed into sand,which is normally a dirtier operation than is conducted for
coatings at brick plants.
f
Support Calculations File: General Shale Moncure CY2016 El
Printed:6/27/2017 Page 27 of 35 Sheet: Dryer(ES-CD-8)

Title: 2016 Air Emission Inventory
Source ID#:ES-VS1,-VS2,-VS3,-VS4,&-VS5
Facility: General Shale Brick,Inc.
Location: Moncure,NC
� Facility ID A 1900009
� Vacuum Systems
i
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 cfm
Bagfilter Efficiency= 99.9%
G-70 Hours of Operation-Cape Fear= - hr/yr
(IES-VS1)
Hours of Operation-Brick Haven: 1,300 hr/yr
(IES-VS2)
1 Total 1.300 hr/yr
G-22 Hours of Operation-Brick Haven= 1,500 hr/yr
i (IES-VS3)-Kiln 3 Hi-Vac
Hours of Operation-Brick Haven: - hr/yr
(IES-VS4&-VS5)
- Total 1,500 hr/yr
Emissions Before Control
PM Emissions=Emissions After Control/(1 -Efficiency)
t PM Emissions= 120.0 lb/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-10 Emissions= 0.120 Ib/hr
PM-2.5 Emissions= 0.120 lb/hr
EMISSION CALCULATIONS
Actual Emissions=PM Emissions,lb/hr(After Control)*Hours of Operation,br/yr
G770(IES-VS 1&-VS2)
Pollutant Actifiq MISS10pS BI3, Actual Em�ss�ons CF" ,, ,Tatal,Act ial Emissions
• Name Ibs/:r•) , ., loos/ r.. x:` (Ibs/yr), ;, (tons/yr) ,;>(lbs/Y<<!')_�' .(tons7yr)F
PM 156.00 0.078 0.00 0.000 156.00 0.078
- PM-10 156.00 0.078 0.00 0.000 156.00 0.078
f PM-2.5 156.00 0.078 0.00 0.000 156.00 0:078
I
G-22(IES-VS3,=VS4&-VS5)
Pollutant Actual Emissions'=VS3 Actual EmrssronsVS4&�'SS Total ActuaL�m�sS�ons
Name . (Ibs/ r. ,• <ltops/ t�., (Ibs/Yr). (Ibs/Y!), (tons/Y!);:
PM 180.00 0.090 0.0.0 0.000 180.00 0:090
PM-10 180.00 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
Support Calculations File: General Shale Moncure CY2016 El
Printed:6/27/2017 Page 28 of 35. Sheet Vacuums(G-22&G-70)

Title: 2016 Air Emission Inventory
Source ID H: Storage Tanks-
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
Note:Emissioins carried over from CY2014.
'Tank
Total
-
`. ; � 'height dsam � Capac>ty ; Throughput �� a ;G � ,�Losses-, Losses ��Em>Isslons°
WN
k!!Yy A
Diesel 1,000 7 5 8'81 66,221 75.14
Gasoline 1'000 7 5 1,028 1,925 1.87
Waste Oil 275 5.25 3 .225 750 3.34
Motor Oil 160 4.5 2.5 129 2,646 20.59
Brick Oil 350 6.5 3 291 3,292 11.321
Gear Oil 350 6.55 3 346 301 ±. 0.87
Support Calculations File:General Shale Moncure GY2016 El
Printed:6/27/2017 Page 29 of 35 'Sheet: Storage Tanks(G-144)

Title: 2016 Air Emission Inventory
Source ID ESBP-FAS
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID 1900009 Did Not Operate in 2016
9afrollcd.f i. t lie
Source
Controlt.
Emission,'. Devicem it
e�t! Co I
;-Factor.,,
u e
Source 0
q,
, �i -Winn) (I t
t ion A
Flyash Sil 3-05-011-06 bin vent 0.0089 0.0049 0.0049 0 0.0013+00 O.00E- 0.00i 0.00E+00 0.0011+00 0.00E+00
.a Controlled PM emission factors for aggregate transfix,pneumatic flyash loading,pneumatic loading of cement silo,neigh hopper loading,and mixer loading from APA2,Section 11.12-
Concrete Batch Operations,(10101).
C,untziill�d
Emission
Fa"
litio'n)
N
Sit o*Hijng,
JHniardous
.Emission
Are [
Example Calculations:
7-
Arsenic 1.0013-06 0.00E+00 0.0011+00 PM Potential Emissions(lbs/yr)
Beryllium 9.0413-08 0.0013+00 0.0011+00 0.0091blton*Olpy-lbs/)T 0 lbstyr
Cadmium 1.98E-08 0.0013+00 0.00E+00
Chnarnitir 1.22E-06 0.00E+00 0.00E+00 PM Potential Emissions(tonslyr) -
Lead 5.20E-07 0.0013+00 0.0011+00 0 lbstyr•(I ton/2000 lb) 0.00E+00 tons/)T
Manganv. 2.56E-07 0.0011+00 0.00E+00
Nickel 2.2811-06 0.0013+00 0.00E+00
Phosphor 3.54E-06 0.0013+00 0.00E+00
Selenium 7.2411-08 0.00E+00 0.0013+00
SupportCalculations File:General Shale Moncone CY2016 El
Printed:642712017 Page 30 of 35 Sheet FN..h Sit.

Title: 2016 Air Emission Inventory
Source ID 4:ES-BP-CS
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID H:1900009
Did Not Operate in 2016
oi'i r
Controlled
Sonrce
'
Emission Entiss n 'Pmi�m ss
.Emission-E';-n Device ID
�Code,;' " 'i'-';Co tro-
ource (SCC) FactorJPastor
"''Pb/ton),� .-
4,...... k9Facfor PM
06)14� I t"(tiii'
Cement S 3-05-011-07 bin vent 0.00099 0.00034 0 0.0013+00 0.00E+00 0.00E+00 0. E+00 0.00E+00 0.00134-00
a Controlled PM emission factors'for aggregate transfer,pneumatic flyash loading,pneumatic loading of'cement silo,weigh hopper loading,and mixer loading from AP42,
Controlled '
bll
Section 11.12-Concrete Batch Operations,(10101).
iiement Ce
ment ......
P, S
sit ssitinsd
Fa-Pus Ftiiitors'
�140fe"�..+- Example Calculations:
Arsenic 4.2412-09 0.00E400 0.00E+00 PM Potential Emissions(lbs/yr)
Beryllium 4.86E-10 0.00F+00 0.00E400 0.00099lb/ton-Olpy--lbs/yr 0 lbsiYr
Cadmium 4.86E-10 0.0013400 0.0013+00
Chrouniur 2.9013-07 0.0013+00 0.00E400 PM Potential Emissions(lonsfyr)
Lead 1.09E-08 0.00E4-00 0.00E+00 0 lbs&-r•(I to.(2000 lb) O.00E+00 lonstyr
Mangan. 1.1713-07 0.00E+00 0.0013-1-00
Nickel 4.18E-05 0.00E-f-00 0.00E+00
Phosphor
Selenium,
Support Calculations File:General Shale Moncure CY2016 El
Printed:6/2712017 Page 31 of 35 Sheet Cement Silo

Title: 2016 Air Emission Inventory
Source ID N: ES-BP-BM[
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID/h 1900009
Did Not Operate in 2016
,ConControlledlid
Source r
Control"
C ';
lassm Ics ition
Devtce Ib
F
0 actor,-'� actor
Emission roughput�,o6ice sl
beicrotion
- tpy) (tpyf 61y) - -it,p i)
Mixer Loading 3-05-011-09 bagfilter 0.011 0.0038 0.0038 0 0.00E+00 0.0013+00 0.00E+00 0-00T7+00 0.00E+00 0.00E+00
a Controlled PM minion factors for aggregate transfer,pmannatictlyash loading,pneumatic loading 917cement silo,neigh hopper loading,and mixer loading from AP-12,Section
11.12-Concrete Batch Operations,(10/01).
M itiw"
&,mjss1oW" a C Uej� Tass
`Hazardous Air $ac Ors Example Calculations:
(t
Arsenic 1,87E-08 0.0000 0.00E+00 PM Potential Emissions(lbs/yr)
Beryllium - - 0.0 11 lb/ton-Otpy--lbsM 0 lbst)r
Cadmium 7.10E-10 0.0000 0.0013+00
Chromium 1.27E-07 0.0000 0.00E+00 PM Potential Emissions(tons/yr)
Lead 3.66E-08 0.0000 0.0013+00 0 lbs/;,•(I to.12000 lb)= 0.0013+00 tos/3,r
Manganese 3.78E-06 0.0000 0.0013+00
Nickel 2.4813-07 0.0000 0.00E+00
Phosphorus 1.2013-06 0.0000 0.00E+00
Selenium - -
Printed:6127/2017 Support Calculations Ffle:General Shale Moncure qY2016 El
Page 32 of 36 Sheet Balch Mixer

EMISSION CALCULATIONS 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 2016
Hours of Operation: 0 hrs
Factors:
Exit Concentration= 0.01 gr/dscf
Flow Rate for System= 5000 efm
Bagfilter Efficiency= 95%
Emissions Before Control
PM/PM-10/PM-2.5 Emissions=Emissions After Control/(1 -Efficiency)
PM/PM-10/PM-2.5 Emissions= .8.6 lb/hr
0.0 lb/yr
0.0 tpy
PM/PM-10/PM-2.5 Emissions=Exit Concentration * 1 lb/7,000 gr*Flow Rate*60 min/hi
PM/PM-10/PM-2.5 Emissions= 0.429 lb/hr
0.00 lb/yr
i
0.00 tpy
Pollutant Contrglled Actual Earussions
Name (lbs'/hr) (ls/yr}a (tons/yr)
PM 4.29E-01 0.00E+00 0.00E+00
PM-10 4.29E-01 0.00E+00 0.00E+00
PM-2.5 4.29E-01 0.00E+00 0.00E+00
Support Calculations File: General Shale Moncure CY2016 El
Printed:6/27/2017 Page 33 of 35 Sheet Rumbler

l
Title: 2016 Air Emissi(
Source 1D M Summary
Facility: General Shale B
Location: Moncure,NC
Emissions Summary
_ !ge Total Total
Pollutant Gas Number Mks';
PM 1.08E+05 54.10
PM-10 1.06E+05 52.85
PM 2.5 1.06E+05 52.83
S02 1.36E+03 0.68
NOx 5.32E+04 26.61
VOC -01 6.66E+03 3.33
CO 1.35E+OS 67.68 Deminimus Report
(lb/yr) (YIN)
5.70E+00 2.85E-03 I TRe off„
1,4-dichlorobenzene 106-46-7 { I
2-butanone(MEK) 78-93-3 { 2.61E+01 1.31E-02 100 No
2-methylphenot(cresol) 95-48-7 { 0.00E+00 0.00E+00 10 No
Acetaldehyde 75-07-0 { 3.87E-06 1.94E-09 10 No
Acrolein 107-02-8 { 4.59E-06 2.29E-09 10 No
Acrylonitrile 107-13-1 { O.00E+00 0.00E+00 10 No
Ammonia 7664-41-7 8.16E-01 4.08E-04 100 No
Antimony 4LNTIMONYCPd, 3.21E+00 1.60E-03 10 No
NT
Arsenic ARSENICCPDS 3.68E+00 1.84E-03 0.01 ,�e MIN
Benzene 71-43-2 ' 3.44E+02 1.72E-01 1 - b '
Benzo(a)pyrene 30-32-8 { 3.06E-07 1.53E-10 1 No
Beryllium BERYLCPDS { 4.99E-02 2.49E-05 1 No
ggw
Bis(2-ethylhexyl)phthalate•'di(2-
117-81-7 2.37E+02 1.19E-01
ethylhexyl)phthalate 10
Bromomethane(Methyl Bromide) 74-83-9 { 0.00E+00 0.00E+00 I No
Cadmium CADMIUMCPD 1.78E+00 8.90E-04 0.1 Ret
Carbon Disulfide 75-15-0 { 5.11E+00 2.55E-03 10 No
Carbon tetrachloride 56-23-5 0.00E+00 0.00E+00 1 No
54E+02 0.08 100
Chlorine 7782-50-5 { 1,• � I
Chloroethane(Ethyl Chororide) 75-00-3 { 6.77E+01 3.38E-02 10
wlw .. .,:
Chloroform 67-66-3 0.00E+00 0.00E+00 t00 No
Chloromethane(Methly Chloride) 74-87-3 7.95E+01 . 3.98E-02 1reort"f
Chromium CROMCPDS { 6.05E+00 3.03E-03 0.01
Cobalt 7440-48-4 { 2.49E-01 1.25E-04 1 No
T Diethylphthalate 84-66-2 2.85E+01 1.42E-02 t an EI pollutant
Dimethylphthalate 131-11-3 0.00E+00 0.00E+00 10 No
Di-n-butylphthalate 84-74-2 1.66E+01 8.31E-03 100 No
Ethylbenzene 100-41-4 5.22E+00 2.61E-03 100 No
Fluorine 7782-41-4 . 0.00E+00 0.00E+00 10 No
Formaldehyde 50-00-0 1.96E+01 9.82E-03 10 e ;p
Hexane I W-54-3 4.59E-01 2.29E-04 100 No
File: General Shale Moncure CY2016 El
Printed:6/27/2017 Sheet: Summary

Fugitive Emission Sources
1 General Shale Brick, Inc (GSB) has identified the emission sources listed below as
fugitive emission sources that are not required to be quantified for fee purposes. The
rationale for determining that these sources are exempt from quantification for fee
purposes is as follows:
1. A brick manufacturing plant is not one of the 26 categories of sources in the list in the
Major Source definition that is required to quantify emissions for applicability
purposes. In accordance with DAQ Rule 15A NCAC 2Q .0202 (1), GSB has not
calculated the fugitive emissions from the sources listed below.
2. The sources listed below are fugitive emission sources defined in the Title V
regulations. Fugitive emissions are defined in the Title V rules (15A NCAC 2Q
.0503 (6) as "those emissions which could reasonably pass through a stack, chimney,
vent, or other functionally-equivalent opening". GSB has determined that the sources
identified below meet the requirements of the fugitive emissions definition.
List of Fugitive Emission Sources
1. Open clay storage piles
2. Clay mining operations
3. Unpaved roads
4. Wet wood receiving, non-pneumatic conveying, and storage operations -
5. One open limestone pile and two open cinder piles and transportation from truck to
piles
6. Coal hopper and coal pile
6/27/2017,FUG-EI-Monc Page 36 of 36

i
Dana Norwell
I _
From: [e-mail]
Sent: Tuesday,June 27, 2017 1219 PM
Subject: Inventory submission confirmation -- 1900009
Dear Dana Norvell
i
Your submittal of the 2016 emission inventory for General Shale Brick, Inc.- Moncure Facility, 1900009, has been
received by the North Carolina Division of Air Quality(DAQ)on June 27,2017 at 12:19:02.You have until the due date of
the emission inventory or two weeks from this submittal to review and repudiate the data submitted.
Please remember to:
-print the Certification Form (see AERO Closeout page),
-have the Responsible Official sign it in blue ink,
-include copies of spreadsheets or calculations used in creating this inventory,and
-mail(postmark) it to NCDAQ,3800 Barrett Drive, Raleigh, NC 27609 by the required due date in order for this
submittal to be considered complete. If you have any questions, please feel free to contact Will Wike, in the Raleigh
Regional Office,at919-791-4200.
The Division of Air Quality thanks you for using AERO,the on line emissions inventory program.
Sincerely
DAQ
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