AQ_F_1900009_20130628_EI_Cmb-EI-File

CY2012 Emission Inventory Review/Data Tracking Form
Check boxes that apply.
Facility Name: E s�4,C &A,y _A46VtjCOff Facility ID: /9oODo 9
Assigned To: STAAI kA111_ ,(Am6 Confidential Request: Yes ❑ No 19
If yes, notify El coordinator and treat as confidential.
Submission type: AERO 19 Paper ❑ If Paper, initials of person entering emissions data into ED
Inventory Review/IBEAM Data Entry
Y N`
All forms appear complete and signed by the appropriate official.
Supporting calculations, control efficiencies,and documentation of emission factors, if not using
AP-42, are included and appear correct.
Pertinent compliance and permitting limits checked and facility is at or below limits (If facility has
exceeded limit, check calculation and explain).
All permitted and known insignificant sources are included and source and control device IDs are
the same as the Ids used in the Air Permit.
All known operating scenarios, control devices, and emission release points have been entered for
each source.
For any pollutant, all emissions have been reported for all permitted and insignificant sources that
contribute to the facility total (above de minimus reporting limits) of that pollutant to the best of
reviewers knowledge.
All volatile HAPS/TAPS included in VOC total. (See pollutant list on DAQ external web page)
Significant changes (>10%)from previous inventories have been investigated and found acceptable
(verified by running QAQC report and Facility Total report in ED-Entry). Print Facility total report and
attach. ✓
Reviewer has checked for facility comments and addressed any issues in the facility comments.
Reviewer has checked for SCCI source type accuracy and corrected errors when found. (please
note errors corrected in summary below). .�
Summary of all changes/additions to inventory:
S i6,uiFic-4Ki- 'dAtv6E_.5 4/1,i�r A dOMBi1V.47iOA/ Zj"V175
o AND40 v�f r. v w� oP��1-r,�. B,Qi c��tav� C/� 4S
-7w&,ao& Ao r wan &P /5.Z% wheat JAPE F�L (1&w /.4tio2
T PoT WA-5l0,0WA/ 62.5 `Z; FAC/e.17l�-W��� BQIGL Ppp�taCT/ n/
VA1.45 DowA! Fir» ZD// wAoz ie 7;ve A7moo.,,vT
d64L Bv/LVFO WAS /J O /07.! o/e
If No, explain corrective action taken in the summary section of this form.
QAQC and Facility Total Reports verified correct? X
Has the Data Entry Complete date been entered in IBEAM? �X (do so only when totally finished)
Signature of Reviewer: �c';k: _.0 = . �t<<, .,,_ Date reviewed: /
(This signature certifies that this review was completed to the best of my ability within the time constraints allowed.)

,�/ N
Facility Total CY 2012 Emission Summary Recorded in ED Facility ID#: 1900009
Facility Name: General Shale Brick, Inc. Moncure Facility Permit#(s): 04384135
Green House Gases Pollutants (GHG) Actual Emissions
Tons/Yr
Demini- Change
Pollutant CAS
mus
Not Not N/A
Reported I Reported
CO2 equivalent(sum of individual GHG pollutant emission No GHGs
times their 1995 IPCC Global Warming Potential(GWP), Reported
converted to metric tons)
Criteria Pollutants Actual Emissions
(Tons/Year)
Pollutant CAS CY 2012 CY 2011 Demini-. %
from ED from Fees mus Change
CO CO 56.59. 76.05 0.5 -25.6 o
NOx' NOx 23.15 26.32 0.5 1-12.0%
PM(TSP)_ TSP 59.38 76.27 0.5 -22.1%
PM10 PM10 44.73 44.63 0.5 0.2%
PM2.5 PM2.5 0.530000 0.800000 0.5 -33.8%
S02 S02 42.03 47.77 0.5 -1.2.0%
VOC VOC 3.03 5.72 0.5 1-47.0%
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPS) (Pounds/Year)
Pollutant CAS CY 2012 CY 2011 Demini- %
from ED from Fees mus Change
Antimony& Compounds(total mass, inc elemental SB) 2.19 2.00 10.0 9.5%
Antimony Unlisted Compounds-Speck Compound SBC-other 2.19 2.00 10.0 9.7%
(Component of SBC)
Arsenic& Compounds (total mass of elemental AS, arsine and 7.42 7.14 0.01 3.9%
all inorganic compounds)
Arsenic Unlisted Compounds-Specify Compound ASC-Other 7.42 7.14 0.01 3.8%
(Component of ASC)
Beryllium & compounds (Total mass) 0.788150 0.694350 1.0 113.5%
Beryllium Metal(unreacted) (Component of BEC) 7440-41-7 0.788150 0.694350 1.0 13.5%
Cadmium& compounds(total mass includes elemental metal) 1.36 1.92 0.1 -29.29
10/15/2013 Page 1"of 4

Facility Total CY 2012 Emission Summary Recorded in ED Facility ID#: 1900009
Facility Name: General Shale Brick,Inc. Moncure Facility Permit#(s): 04384T35
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPs) . (Pounds/Year)
Pollutant CAS CY 2012 CY 2011 Demini- %
from ED from Fees mus Change
Cadmium Metal, elemental, unreacted(Component ' 7440-43-9 1.36 1.92 0.1 -29.2%
of CDC)
Chromium-All/Total(includes Chromium (VI) categories, 4.43 5.47 0.1 -19.0%
metal and others)
Chromic acid(VI) (Component of SolCR6& CRC) 7738-94-5 4.43 5.47 0.01 1-19.0%
Chromium (VI) Soluble Chromate Compounds(Component of 4.43 5.47 0.01 -19.0%
CRC)
Chromic acid(VI) (Component of SolCR6&,CRC) 7738-94-5 4.43 5.47 0.01 1-19.0%
Cobalt& compounds 0.168800 0.146550 1.0 15.2%
i
Cobalt Unlisted Compounds-Specify Compound COC-other 0.168800 0.146550 1.0 15.2%
(Component of COC)
Lead& compounds 12.89 15.23 1.0 -15.4%
Lead Unlisted Compounds-Specify Compound PBC-Other 12.89 15.23 10.0 -15.4%
(Component of PBC)
Manganese& compounds 26.64 39.40 10.0 -32.4%
Manganese Unlisted Compounds-Specify MNC-other 26.64 39.40 10.0 -32.4%
Compound(Component of AMC)
Mercury& Compounds-all total mass includes Hg Vapor 4.95 4.67 0.001 6.0%
Mercury, vapor (Component of HGC) 7439-97-6 4.95 4.67 0.001 6.0%
Nickel& Compounds,sum total mass includes elemental 6.02 6.54 1.0 -8.0%
Nickel metal(Component of NIQ 7440-02-0 6.02 6.54 1.0 -8.0%
Polycyclic Organic Matter(Specific Compounds from OAQPS 2.42 2.10 1.0
or Ti9 115.2%
Naphthalene (Component of 83329/POMTV) 91-20-3 2.42 2.10 1.0 15.2%
Acrylonitrile 107-13-1 0.131800 0.753940 10.0 -82.5%
Benzene 71-43-2 111.08 115.32 1.0 -3.7%
Carbon disulfide 75-15-0 1.62 2.01 10.0 -19.3%
Carbon tetrachloride 56-23-5 0.010680 0.022060 1.0 -51.6%
10/15/2013 Page 2 of 4

Facility Total CY 2012 Emission Summary Recorded in ED Facility ID#: 1900009
Facility Name: General Shale Brick,Inc.Moncure Facility Permit#(s): 04384135
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants(TAPS) (Pounds/Year)
Pollutant CAS CY 2012 CY 2011 Demini- %
from ED from Fees mus Change
CFC-11 (Trichlorofluoromethane) 75-69-4 1.14 1.02 100.0 11.8%
Chlorine 7782-50-5 104.50 90.72 100.0 15.2%,
Chloroform 67-66-3 0.010680 0.022060 100.0 -51.6%
DEHP (Di(2-ethylhexyl)phthalate) 117-81-7 68.77 64.46 10.0 6.7%
Dibutylphthalate 84-74-2 11.36 10.40 100.0 9.2%
Dichlorobenzene(p), 1,4- 106-46-7 1.70 1.47 1.0 115.6%
Dimethyl plithalate 131-11-3 0.062720 0.054500 10.0 115.1%
Ethyl benzene 100-41-4 2.50 2.51 100:0; -0.3%
Ethyl chloride (chloroethane) 75-00-3 18.90 16.40 10.0. 15.2%
Fluorides(sum of all fluoride compounds as mass of B6984-48-8 7,459.82 18,862.61 10.0 -60.5016 f
ion)
Formaldehyde 50-00-0 22.41 88.81 IO.Or= -74.8% T
Hekane,n- 110-54-3 0.176400 0.176400 - 100:('' 0.0%
Hydrogen chloride (hydrochloric acid) 7647-01-0 5,855.59 10,805.77 100.0 -45.8%
Hydrogen fluoride(hydrofluoric acid as mass of HF) 7664-39-3 4,659.31 11,786.63 100.0 -60.5%
(Component of 16984488/Fluorides)
MEK(methyl ethyl ketone, 2-butanone) 78-93-3 20.63 25.33 100.0 -18.6%
Methyl bromide(bromomethane) 74-83-9 2.23 3.42 1.0 -34.7%
Methyl chloride(chloromethane) -74-87-3 36.51 78.85 1.0 -53.7%
Methyl chloroform 71-55-6 0.974610 0.863630 100.0 12.9%
Methyl iodide (iodomethane) 74-88-4 9.14 16.01 10.0 -42.9%°
Methylene chloride 75-09-2 0.494390 2.52 1.0 -80.4%
Perchloroethylene (tetrachloroethylene) 127-18-4 0.227710 0.210480 100.0 8.2%
Phenol 108-95-2 5.14 7.84 100.0 -34.4%
Phosphorus Metal, Yellow-or White 7723-14-0 82.62 90.26 1.0 -8.5%
Selenium Compounds SEC -18.81 17.92 10.0 5.0%
Styrene 100-42-5 _ 0.677140 0.728660 100.0 -7.1%
10/15/2013 Page 3 of 4

Facility Total CY 2012 Emission Summary Recorded in ED Facility ID#: 1900009
Facility Name: General Shale Brick, Inc. Moncure Facility Permit#(s): 04384T35
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPS) (Pounds/Year)
Pollutant CAS CY 2012 CY 2011 Demini- %
from ED from Fees mus Change
Toluene 108-88-3 20.18 31.96 100.0 1-36.9%
Vinyl acetate 108-05-4 0.009360 0.014520 100.0 1-35.5%
Xylene (mixed isomers) 1330-20-7 12.85 12.34 100.0 4.1%
Xylene, o- 95-47-6 4.18 3.88 100.0 7.8%
Largest Individual HAP Hydrogen chloride(hydrochloric acid) 5,855.59 lbs
Total HAP Emissions 1,121.47 lbs
DAQ's Comments Regarding Inventory
The amount of coal fired in 2012 was 107.6%higher than the amount burned in 2011. The throughput for the Cape Fear
plant was 82.5%lower than the throughput in 2011. The throughput for the Brickhaven plant was 15.2%higher than the
throughput in 2011. Facility-wide production was down 20.23%from the production in 2011.
10/15/2013 Page 4 of 4

I
I
I
I
..........................At.....................................................................................................
.................................... ....... .......-
2012 CALENDAR YEAR EMISSIONS INVENTORY
IGeneral Shale Brick, Inc. - Moncure, NC Facility
General Shale Brick
Building The American Dream'
I
I
I
June 2013
IProject 133401.0017
IPrepared By:
' TRINITY CONSULTANTS
One Copley Parkway
Suite 310
Mooresville,NC 27560
[phone]
n i /�
Ly
I
ConTslultalits
Environmental solutions delivered uncommonly well
I

WoodFuel/Sawdust System(New) ... .................................................................................................. ................................16
ClayHandling Equipment...................................................................................:................................................................................20
IntersiteConveyer......................... ...._.._..............................._---_.._.._. -- --- .- . ... - . .22_
BrickTexturing.......................................................................................................................................................................................24
CoatingsDryer.........................................................................................................................................................................................25
VacuumSystem.......................................................................................................................................................................................28
_ Storage Tanks..........................................................................................................................................................................................29
FlyashSilo.................................................................................................................................................................................................30
CementSilo...............................................................................................................................................................................................31
BatchMixer...............................................................................................................................................................................................32
Rumbler.............................................................................................................:.......................................................................................33
Summaryof Emissions.........................................................................................................................................................................34
FugitiveSources......................................................................................................................................................................................36
APPENDIX A: TANKS 4.09 CALCULATIONS
i
General Shale Brick, Inc. -Moncure, NC Facility I CY 2012 Emissions Inventory
Trinity Consultants

SECTION 1
NCDAQ CY 2012 EMISSION INVENTORY (AERO) FORMS
General Shale Brick, Inc. -Moncure, NC Facility I CY 2012 Emissions Inventory
Trinity Consultants

Original COPY of RECORD Date Submitted: 6/27/2013 11 :51 :25
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 2012
These forms must be completed and returned even if the facift did not operate or emissions were zero
The legally defined "Responsible Official" of record for your facility is Charles Smith
This person or one that meets the definition below must sign this certification form.
The official submitting the information must certify that he/she complies with the requirements as specified in Title 15A
NCAC 2Q.0520(b)which references and follows the federal definition.40 CFR Part 70.2 defines a responsible as meaning one
of the following:
1.For a corporation:a president,secretary,treasurer,or vice--president of the corporation in charge of a principal
business function,or any other person who performs similar policy or decision making functions for the overall
operation of one or more manufacturing,production,or operating facilities applying for a or subject to a permit and
either
i.the facilities employ more than 250 persons or have gross annual sales or expenditures exceeding$25
million(in second quarter 1980 dollars);or
ii.the delegation of authority to such representatives is approved in advance by the permitting authority;
2.For partnership or sole propietorship;a general partner or the proprietor,respectively;
3. for a muncipality,state,federal,or other public agency includes the chief executive officer having responsibility for the
overall operations of a principal geographic unit of the agency(e.g.,a Regional Administrator of EPA).
ERTIFICATION STATEMENT
frnportatic Legally Responsible Official,relld and 5ign after all sljbinissignsgre
certify that I am the responsible official for this facility,as described above,and hereby certify that the information contained
n 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 Sieved: ZB Mj"r �z 1
Printed Name: Charles Smith.
Signature: (�/y
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
Original COPY of RECORD Date Submitted: 6/27/2013 11:51:25 1

Original COPY of RECORD Date Submitted: 6/27/2013 11 :51 :25
- As entered in AERO
Facility Name: General Shale Brick,Inc.Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit: 04384
Moncure,NC 27559 County: Chatham
DAQ Region : RRO
Listing of Emission Sources and Control Devices on Permit. See instructions
ES ID on Air ES Description CS ID CS Description CD ID's
Permit -
ES—BP—BM batch mixer(39.97 tons per hour - CS-12 one bagfilter(535 sgaure CD—BP—BH1
capacity) feet of filter area),
cement silo(10 tons per hour one bin vent filter(227
ES—BP—CS CS-13 CD—BP—BV2
capacity) square feet of filter area),
ES—BP—FAS flyash silo(11 tons per hour CS-14 one bagfilter(535 sqaure CD—BP—BHl
- capacity) feet of filter area),
Natural gas—fired rotary drum
ES—CD-8 coatings dryer(250,000 Btu per
hour maximum heat input;3.45
tons per hour capacity)
bagfilter(6,096 square feet
of filter area),Bagfilter,
(6,096 square feet of filter CD—CR6BF,.CD—CR7BF,
ES—CR5 Texturizing operation for Line 1 CS-19 area),bagfilter(4,062 square CD—CR7BF2,CD—CR7BF3
feet of filter area),bagfilter
(3,040 square feet of filter
area),
bagfilter(6,096 square feet
of filter area),Bagfilter
(6,096 square feet of filter CD—CR6BF,CD—CR7BF,
ES—CR6 Texturizing operation for Line 2 CS-19 area),bagfilter(4,062 square CD—CR7BF2,CD—CR7BF3
feet of filter area),bagfilter
(3,040 square feet of filter
area),
bagfilter(6,096 square feet
of filter area),Bagfilter
Texturizing operation for Lines (6,096 square feet of filter CD—CR6BF,CD—CR7BF,
ES—CR7 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
-- ES—Coal—CC coal crusher CS-18 bagfilter(air to cloth ration CD—Coal—CC
of 4.7 to 1),
ES—Kl Wood/natural gas—fired tunnel CS-8 Two Simple cyclones(89 CD—CI,CD—C2
brick kiln(20.3 million Btu per inches in diameter)
2

hour maximum heat input and
13.7 tons per hour maximum
fired brick production rate)
[Case By Case MACT]
Wood/natural gas—fired tunnel
brick kiln(20.3 million Btu per
ES—K2 hour maximum heat input and CS-8 Two Simple cyclones(89 CD—C 1,CD—C2
13.7 tons per hour maximum inches in diameter)
fired brick production rate)
[Case By Case MACT]
Natural gas/propane—fired brick
ES—K3D1 dryer(4.43 million Btu per hour
heat input)
Natural gas/propane—fired brick
ES—K3D2 dryer(4.43 million Btu per hour
heat input)
Natural gas/propane—fired brick
ES—K3D3 dryer(4.43 million Btu per hour
heat input)
Coal/natural gas/propane—fired
brick tunnel kiln(25.9 million
ES—K3K Btu per hour maximum heat CS-15 dry limestone adsorber, CD—K3DLA
input and 20.55 tons per hour
maximum fired brick production
rate)[Case By Case MACT]
Natural gas/propane—fired brick
ES—K4D 1 dryer(4.43 million Btu per hour
maximum heat input)
ES—K4132 Natural gas/propane—fired brick
dryer(4.43 million Btu per hour)
ES—K4D3 Natural gas/propane—fired brick
dryer(4.43 million Btu per hour)
Coal/natural gas/propane—fired
brick tunnel kiln(25.9 million
ES—K4K Btu per hour maximum heat CS-11 dry limestone adsorber, CD—K4DLA
input and 20.55 tons per hour
maximum fired brick production
rate) [Case By Case MACT]
ES—RUMBLE rumbler system
ES—SS Sand Storage Silo
rotary sawdust dryer(5.59 tons
per hour drying capacity;heated Two Simple cyclones(89
ES—WD1,2 by recycle heat from kilns 1 and CS-8 inches in diameter) CD—C1,CD—C2
2 with natural gas used as a
supplemental fuel)
ES—WFS—SD—CV 1 Transfer screw conveyor CS-17 dust collector(air to cloth CD—SD—DC 1,CD—SD—DC2,
ratio of 8.17 to 1),dust ES—WFS—SD—CYC,
collector(air to cloth ratio of CD—SD—BV 1, CD—SD—BV2
8.06 to 1),cyclone(42 inches
in diameter),bin vent filter
(air to cloth ratio of 4.44 to
3

1),bin vent filter(air to cloth
- - - - - ratio of 4.44-to 1)-------
dust collector(air to cloth
ratio of 8.17 to 1),dust
collector(air to cloth ratio of CD-SD-DC1,CD-SD-DC2,
ES-WFS-SD-CV2 Screen feed screw conveyor CS-17 8.06 to 1),cyclone(42 inches ES-WFS-SD-CYC,
in diameter),bin vent filter CD-SD-BV 1, CD-SD-BV2
(air to cloth ratio of 4.44 to
1),bin vent filter(air to cloth
ratio of 4.44 to 1),
dust collector(air to cloth
ratio of 8.17 to 1),dust
collector(air to cloth ratio of CD-SD-DC I,CD-SD-DC2,
ES-WFS-SD-CV3 Enclosed conveyor CS-17 8.06 to 1),cyclone(42 inches ES-WFS-SD-CYC,
in diameter),bin vent filter CD-SD-BV1, CD-SD-BV2
(air to cloth ratio of 4.44 to
1),bin vent filter(air to cloth
ratio of 4.44 to 1),
dust collector(air to cloth
ratio of 8.17 to 1),dust
collector(air to cloth ratio of CD-SD-DC I,CD-SD-DC2,
i
ES-WFS-SD-CYC Cyclone CS-17 in
to 1),cyclone
n e vent n filter inches ES-WFS-SD-CYC,
n diameter),bin CD-SD-BV 1, CD-SD-BV2
(air 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,
m
8.06 to 1),cyclone(42 inches
ES-WFS-SD-HM hamermill CS-17 ES-WFS-SD-CYC,
in diameter),bin vent filter CD-SD-BV1, CD-SD-BV2
(air to cloth ratio of 4.44 to
1),bin vent filter(air to,cloth
ratio of 4.44 to 1),
dust collector(air to cloth
ratio of 8.17 to 1),dust
collector(air to.cloth ratio of CD-SD-DC 1,CD-SD-DC2,
ES-WFS-SD-SC1 8x8 screen CS-17 8.06 to 1),cyclone(42 inches ES-WFS-SD-CYC,
in diameter),bin vent filter CD-SD-BV 1,CD-SD-BV2
(air to cloth ratio of 4.44 to
1),bin vent filter(air to cloth
ratio of 4.44 to 1), -
dust collector(air to cloth
ratio of 8.17 to 1),dust
collector(air to cloth ratio of CD-SD-DC 1,CD-SD-DC2,
8.06 to 1),cyclone(42 inches
ES-WFS-SD-SC2 8x8 screen CS-17 ES-WFS-SD-CYC,
in diameter),bin vent filter CD-SD-BV 1,CD-SD-BV2
(air to cloth ratio of 4.44 to
1),bin vent filter(air to cloth
ratio of 4.44 to 1),
-- ES-WFS-SD-SDS Sawdust silo CS-17 dust collector(air to cloth CD-SD-DC 1,CD-SD-DC2,
ratio of 8.17 to 1),dust ES-WFS-SD-CYC,
collector(air to cloth ratio of CD-SD-BV 1,CD-SD-BV2
4

i
J 8.06 to 1),cyclone(42 inches
in diameter),bin vent--filter
--- -- - ---- -
(air to cloth ratio of 4.44 to
1),bin vent filter(air to cloth
ratio of 4.44 to 1),
dust collector(air to-cloth
ratio of 8.17 to 1),dust
- collector(air to cloth ratio of CD—SD—DC I, CD—SD—DC2,
ES—WFS—SD—SH Surge hopper CS-17 8.06 to 1),cyclone(42 inches ES—WFS—SD—CYC,
in diameter),bin vent filter CD—SD—BV1,CD—SD—BV2
(air 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 40
CFR Part 60 Subpart 000]
F—CH—BC Brickhaven conveyor[NSPS 40
CFR Part 60 Subpart 000]
F—CH—Cl 1 Impact crusher[NSPS 40 CFR
Part 60 Subpart 000]
F—CH—CFC Cape Fear conveyor[NSPS 40
CFR Part 60 Subpart 000]
F—CH—FC Feed Conveyor[NSPS 40 CFR
Part 60 Subpart 000]
F—CH—FS 1 Finishing screen[NSPS 40 CFR
Part 60 Subpart 000]
F—CH—FS2 Finishing screen[NSPS 40 CFR
Part 60 Subpart 000]
F—CH—FS3 Finishing Screen[NSPS 40 CFR
i Part 60 Subpart 000]
F—CH—FS4 Finishing screen[NSPS 40 CFR
Part 60 Subpart 000]
F—CH—H1 Hammennill NSPS [40 CFR
Part 60 Subpart 000]
F—CH—H2 Hammennill[NSPS 40 CFR
Part 60 Subpart 000]
F—CH—P1 product conveyor[NSPS 40
CFR Part 60 Subpart 000]
F—CH—P2 product conveyor[NSPS 40
CFR Part 60 Subpart 000]
F—CH—RC reversing conveyor[NSPS 40
_ CFR Part 60 Subpart 000]
F—CH—SFC1 Screen feed conveyor[NSPS 40
CFR Part 60 Subpart 000]
F—CH—SFC2 Screen feed conveyor[NSPS 40
CFR Part 60 Subpart 000]
F—CH—SFC3 Screen feed conveyor[NSPS 40
CFR Part 60 Subpart 000]
F—CH—SFC4 Screen feed conveyor[NSPS 40
CFR Part 60 Subpart 000]
5

i
F—CH—SS1 Scalping screen[NSPS 40 CFR
Part 60 Subpart 000]
F—CH—SS2 Scalping Screen[NSPS 40 CFR
Part 60 Subpart 000]
F—CH—SSFC scalping conveyor[NSPS 40
_ CFR Part 60 Subpart 000]
- F—CH—T1 tallings conveyor[NSPS 40
CFR Part 60 Subpart 000]
F—CH—T2 tallings conveyor[NSPS 40
_ CFR Part 60 Subpart 000]
F—CH—TC1 Trampolin Conveyor[NSPS 40
CFR Part 60 Subpart 000]
F—CH—TC2 Trampolin Conveyor[NSPS 40
CFR Part 60 Subpart 000]
F—FC4 Finishing conveyor#4 [NSPS—
40 CFR Part 60 Subpart 000]
Finishing conveyor#5 [NSPS—
F—FCS 40 CFR Part 60 Subpart 000]
F—FS 1 Single deck finishing screen
[NSPS Subpart 000]
F—FS2 Single deck finishing screen
[NSPS Subpart 000]
F—FS3 finishing screen[NSPS Subpart
000]
F—FS4 finishing screen[NSPS Subpart
000]
F—FS5 Finishing screen
F—FS6 Finishing screen
F—FS7 Finishing screen
F—FS8 Finishing screen
F—FS9 Finishing Screen
F—HM.12A Hammermill[NSPS—40 CFR
Part 60 Subpart 000]
F—PC Primary crusher[NSPS—40
CFR Part 60 Subpart 000]
F—SGS secondary crusher[NSPS 000]
F—SS1 Scalping Screen[NSPS Subpart
000]
F—SS2 Scalping Screen[NSPS Subpart
000]
Hammermill Feed Conveyor
FCH—HFC1 [NSPS 40 CFR Part 60 Subpart
000]
Hammermill Feed Conveyor
FCH—HFC2 [NSPS 40 CFR Part 60 Subpart
000]
I—ES—K1D1 brick dryer associated with Kiln
6

I—ES—K2D1 brick dryer associated with Kiln
2
i
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
IES—F—CH6 Existing raw material handling
and conveying operations
IES—F—CO-2 Reclaimer(coating operations)
IES—F—CO—Cl Conveyor(coating operation)
IES—F—CO—C2 Conveyor(coating operation)
IES—F—CO—C3 Conveyor(Coating operation)
IES—F—CO—C4 Conveyor(Coating operation)
-.-i IES—F—CO—CS Conveyor(coating operation)
IES—K4F.1 Box feeder for Line 4
IES—K4F.2 conveying system for line 4
IES—K4F.3 storage tank for line 4
IES—RECLAIM Reclaimer building storage piles
Wood receiving,non—pneumatic
IES—SD 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—TS 1,000 gallon gasoline storage
tank
Package—type kiln car Two Bagfilters(97 square
IES—VS1 CS-10 feet and 297 square feet of CD—VS1,CD—VS2
vacuuming system
filter area)
Package—type kiln car Two Bagfilters(97 square
IES—VS2 CS-10 feet and 297 square feet of CD—VS1,CD—VS2
vacuuming system filter area)
IES—VS3 Hi—Vac vacuum system for Kiln
3
IES—VS4 package—type kiln car
vacuuming system
IES—VS5 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 propane vaporizer(1.3 million
Btu per hour per burner)
7

Screened Clay Conveying and
IS-3 Handling Operation for Kiln 1
and 2
Screened clay conveying and
IS-4 handling operation for Kiln 3
and 4
IS-7.1. sand coating pile
IS-7.2 sand coating pile
IS-7.3 sand coating pile
IS-7.4 sand coating pile
IS-7.5 sand coating pile
IS-7.6 sand coating pile .
IS-7.7 conveyor
IS-7.8 conveyor
IS-8.1 Kiln 3 storage pile
IS-8.2 Kiln 3 box feeder
IS-8.3 Kiln 3 storage bin
IS-8.4 Kiln 3 conveyor
IS-8.5 Kiln 3 conveyor
IS-8.6 Kiln 3 conveyor
IS-8.7 Kiln 3 conveyor
IS-8.8 Kiln 3 conveyor
IS-8.9 Kiln 3 conveyor
i ,
t
8

Original COPY of RECORD Date Submitted: 6/27/2013 11 :51 :25
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
i
DAQ Region : RRO
Emission Source & Operating Scenario List- See Instructions
ES Group ID ES ID OS ID OS Description
GR12 ES-K3D1,ES-K3D2,ES-K3D3 20 Natural gas/propane-fired dryers
for Kiln 3
ES-WFS-SD-CV1,ES-WFS-SD-CV2,
ES-WFS-SD-CV3, ES-WFS-SD-CYC,
GR21 ES-WFS-SD-HM,ES-WFS-SD-SC 1, 30 Wood Fuel/Sawdust System
ES-WFS-SD-SC2,ES-WFS-SD-SDS,
ES-WFS-SD-SH
GR22 IES-VS3,IES-VS4,IES-VS5 35 Vacuum Systems-Brickhaven
G-66 ES-K1,ES-K2,ES-WD1,2 14 Wood/natural gas-fired brick kilns
and green brick dryer(Cape Fear)
- G-69 ES-CR5,ES-CR6,ES-CR7 37 Texturizing Operations
- G-70 IES-VS1,IES-VS2 34 Vacuum System
j' F-C-CFBH,F-FC4,F-FC5,F-FS1,
F-FS2,F-FS3,F-FS4,F-FS5,F-FS6, Primary Clay Grinding and
G-7i F-FS7,F-FS8,F-FS9,F-HM.12A,F-PC, 31 Screening Operation
F-SS1,F-SS2
G-72 I-ES-K1D1,I-ES-K2D1 15 Dryers associated with Kilns 1 and.
2
F-CH-BC,F-CH-C1,F-CH-CFC,,
F-CH-FC,F-CH-FS1,F-CH-FS2,
F-CH-FS3,F-CH-FS4,F-CH-H1,
F-CH-H2,F-CH-P 1,F-CH-P2,
G-132 F-CH-RC,F-CH-SFC1,F-CH-SFC2, NONE NONE
F-CH-SFC3,F-CH-SFC4,F-CH-SS1,
F-CH-SS2,F-CH-SSFC,F-CH-TI,
F-CH-T2,F-CH-TC1,F-CH-TC2,
FCH-HFC 1,FCH-HFC2
G Natural gas/propane-fired dryers
-135 ES-K4D1,ES-K4D2,ES-K4D3 29
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-Cl,IES-F-CO-C2,
IES-F-CO-C3,IES-F-CO-C4,
IES-F-CO-05,IES-K4F.1,IES-K4F.2,
IES-K4F.3,IES-RECLAIM,
IF-BH-MR-C,IF-BH-MR-DH,IS-3,
IS-4,IS-7.1,IS-7.2,IS-7.3,IS-7.4,
IS-7.5,IS-7.6,IS-7.7,IS-7.8,IS-8.1,
9

IS-8.2,IS-8.3,IS-8.4,IS-8.5,IS-8.6,
- IS-8.7,IS-8.8,IS-8.9
G-144 IES—T1,IES—T2,IES—T3,IES—T4, 18 Storage tanks
IES—T5
ES—BP—BM 26 Batch Mixer
- ES—BP—CS 27 Cement Silo
ES—BP—FAS 28 Flyash Silo
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 tuinbles blocks in a
rotating drum in order to create an
ES—SS NONE NONE
F—SGS NONE NONE
I—F—Coal—CH NONE NONE
I—F—Coal—CP NONE NONE
I—F—SSC NONE NONE
IES—SD NONE NONE
- IS-14 19 Propane Vaporizer
10

Original COPY of RECORD Date Submitted: 6/27/2013 11 :51 :25
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 2012
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
3. Operating Scenario ID/Description: OS—20/Natural gas/propane—fired dryers for Kiln 3
4. SCC Number/Description: 30500351Brick Manufacture—Dryer; Brick Dryer: Heated With Waste Heat
And Supplemental Gas Burners
5. Throughput/units in 2012:
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
ERP for ES—K3K,
EP—K3 VERTICAL STACK 35 4.92 99.95 33.79 38544.24 ES—K3D1 AND
ES—K3D2
11

Operating Scenario: OS—20 Emission Source/Group ID: GR12
10,Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2012)
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 hut:
an—Feb +Dec o arch—May o �une—Aug. o �ept.—N6v. o
_ 20n 25/0 012 25/o" 012 25/0 012 25/o
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2012
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po�ant Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2012
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 . 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP Emissions Emission Control
Pollutants (In CAS HAP/TAPS Estimation Emission
(see instructions) Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2012
- ,I
12

Original COPY of RECORD Date Submitted: 6/27/20.13 11 :51 :25
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 2012
1. Emission Source ID (from permit)or Group GR21 consisting of ES—WFS=SD—CV 1, ES—WFS—SD—CV2,
-_ Emission Source Group ID ES—WFS—SD—CV3,ES—WFS—SD—CYC,ES—WFS—SD—HM,
ES—WFS—SD—SC 1,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: 30500305/Brick Manufacture—Material Prep ;Raw Material Handling and
Transferring
5. Throughput/units in 2012: 160 HR/yr
(e.g.production or fuel use):
- 6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-17 ` CD—SD—DC1 dust collector air to cloth ratio of 8.17 to 1
2 CS-17 CD—SD—DC2 dust collector air to cloth ratio of 8.06 to 1
3 CS-17 ES—WFS—SD—CYC cyclone 42 inches in diameter
4 CS-17 CD—SD—BV 1 bin vent filter air to cloth ratio of 4.44 to 1
5 CS-17 CD—SD—BV2 bin vent filter air to cloth ratio of 4.44 to 1
9.Emission Release Point RP Information: Sources vented to more than one ERP use additional entry lines):
ERP II) ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feetlsec) Rate(Acfm)
Rectangle(L x Vie
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
WoodfueP—SD—DC2 VERTICAL STACK 20 1 72 49.76 2345 System Sawdust
- System Screens
Conveyors
P—SD—BV2 VERTICAL STACK 20 0.5 75 33.95 400 Bin Vent on Surge
Hopper
Dust Collector on
P—SD—DC1 VERTICAL STACK 20 1 72 44.56 2100 Woodfuel Sawdust
System Screens
Conveyors
}
4
i
14

Operating Scenario: OS—30 Emission Source/Group ID: GR21
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2012)
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"�o une—Aug. 25"�u Sept.—Nov. 25%
2012 012 012 012
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS v GHG Estimation' Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2012
I -
I -
Criteria Emissions— Emission Control
Pollutant. Criteria Estimation Efficiency Emission
��QS) Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2012
CO CO 08 0
NOx NOx 08 0
TSP TSP 0.04 08 99
PM10 PM10 0.04 08 99
PM2.5 PM2.5 0.04 08 . 99
S02 S02 08 0
VOC VOC 08 0
HAP/TAP CAS Emissions Emission Control
Pollutants (In HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2012
F
i
i
15

i I -
Original COPY of RECORD Date Submitted: 6/27/2013 11 :51 :25
--' 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 2012
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
r-
3. Operating Scenario ID/Description: OS—35/Vacuum Systems—Brickhaven
4. SCC Number/Description: 30500317/Brick Manufacture—Material Prep ; Raw Material Unloading
5. Throughput/units in 2012: 1920 HR/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
i 7. Capture Efficiency
(%of Emissions from this Process Vented to Control
_ Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
I .
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
I j ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) ` (Feet/sec) Rate(Acfm)
Rectangle(L x
W)
in 0.1 feet)
EP—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
EP—VS5 DOWNWARD—FACING VENT 1 3 72 3.3F1400 Emission point for
` IES—VS5
16

- Operating Scenario: OS—35- Emission Source/Group ID: GR22
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2012)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:.
an—Feb +Dec 25% arch—May 250�o run,,e—Aug. 25"�o �012
ept.—Nov. 25%
2012 012
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
Tons/Year See Instructions all controls
2012
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)
- 2012
CO CO 08
NOx NOx 08
TSP TSP 0.12 08
PM10 PM10 0.12 08
PM2.5 PM2.5 0.12 08
S02 S02 08
VOC VOC 08
_c HAP/TAP CAS Emissions Emission Control
HAP/TAPS Estimation Emission
Pollutants (In
(see instructions) Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2012
17

Original COPY of RECORD Date Submitted: 6/27/2013 11 :51 :25
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 2012
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
3. Operating Scenario ID/Description: OS— 14/Wood/natural gas—fired brick kilns and green brick dryer(Cape Fear)
4. SCC Number/Description: 3050036IBrick Manufacture—Dryer; Sawdust Dryer: Heated With Exhaust
From Sawdust—fired Kiln
5. Throughput/units in 2012: 6937 TON/yr
(e.g.production or fuel use):
6. Fuel Information (if fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
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 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#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
(in 0.1 feet)
ERP for ES—K1,
- EP—Cl VERTICAL STACK 65 2.5 150 53 15609.78 ES—K2,and
ES—SDI
ERP for ES—Kl,
EP—C2 VERTICAL STACK 65 2.5 150 53 15609.78 ES—K2,and
ES—SDI
18

Operating Scenario: OS— 14 Emission Source/Group ID: G-66
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2012)
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%
arch—May 25%
2012 012 �012
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emission
Emissions— Estimation Control
GHG CAS GHG Method Efficiency Emission Ef Control
Pollutants Pollutants Code (Net after Factor
(Tons/Year) (See all controls)
Instructions
2012
Emission
Criteria Emissions— Estimation Control
Pollutant Criteria Method Efficiency Emission
Po�QS Code Pollutants .Code (Net afte Factor Ef Control
Pollutantss
(Tons/Year) (See all controls)
Instructions
2012
CO CO 1.19 08 0 0.344 AFTER
NOx NOx 1.28 08 0 0.37 AFTER
TSP TSP 2.34 08 85 0.675 AFTER
PM10 PM10 2.34 08 85 0.675 AFTER
PM2.5 PM2.5 2.34 08 85 0.675 AFTER
S02 S02 0.64 08 0 AFTER
VOC VOC 0.62 08 0 0.18 AFTER
Emission
Emissions Estimation Control
HAP/TAP CAS HAP/TAPS Method Efficiency Emission EF Control
Pollutants (In Alphabetical Order) (see instructions) (Pounds/Year) Code (Net after all Factor
(See controls)
Instructions
2012.
Acr lonitrile 107-13-1 0.1318 08 0 0.000019 AFTER
Antimony Unlisted Compounds(Specify SBC—Other 0.01942 08 0 0.0000028 AFTER
Component of SBC
Arsenic Unlisted Compounds(Specify ASC—Other 0.14568 - 08 0 0.000021 AFTER
Component of ASC
Benzene 71-43-2 3.88472 08 0 0.00056 AFTER
Beryllium metal(unreacted) 7440-41-7 0.00215 08 0 3.1E-7 AFTER
(Component of BEC
CFC-11 richlorofluoromethane 75-69-4 0.00694 08 0 0.000001 AFTER
7440-43-9 0.15261 08 0 0.000022 AFTER
20

Cadmium Metal(elemental unreacted,
- Component of CDC
Carbon disulfide 75-15-0 0.12487 08 0 0.000018 AFTER
Carbon tetrachloride 56-23-5 0.00264 08 0 3.8E-7. AFTER
Chloroform. 67-66-3 0.00264 08 0 3.8E-7 AFTER
Chromic acid(VI)(Component of 7738-94-5 0.33298 08 0 0.006048
So1CR6 CRC
' Di 2-eth lhex 1 hthalate EHP 117-81-7 0.97118 08 0 0.00014 AFTER
Dibu I hthalate 84-74-2 0.11099 08 0 0.000016 AFTER
Dimeth 1 phthalate 131-11-3 0.00002 08 0 2.4E-9 AFTER
Eth 1 benzene 100-41-4 0.06937 08 0 0.00001 AFTER
Fluorides(sum of all fluoride 16984-48-8 1872.99 04 0 0.27 AFTER
r
compounds)
Formaldehyde 50-00-0 17.97 10 0 AFTER
Hydrogen chloride(hydrochloric acid 7647-01-0 1179.29 08 0 0.17 AFTER
Hydrogen fluoride(hydrofluoric acid as 7664-39-3 1595.51 04 0 0.23 AFTER
mass of HF-Component of Fluorides
'- Lead Unlisted Compounds(Specify and PBC-Other 0.83244 08 0 0.00012 AFTER
Component of PBC
Manganese Unlisted Compounds MNC-Other 3.32976 08 0 0.00048 AFTER
(Specify Component of MNC
Mercury,vapor(Component of HGC 7439-97-6 0.07631 08 0 0.000011
Methyl,bromide 74-83-9 0.30523 08 0 0.000044 AFTER
Methyl chloride 74-87-3 9.7118 08 0 0.0014 AFTER
Meth l chloroform 71-55-6 0.00361 08 0 5.2E-7 AFTER
Methyl ethyl ketone 78-93-3 1.52614 08 0 0.00022 AFTER
Methyl.iodide 74-88-4 1.66488 08 0 0.00024 AFTER
Methylene chloride 75-09-2 0.43009 08 0 0.000062 AFTER
Naphthalene(Component of POM 91-20-3 0.00002 08 0 2.4E-9 AFTER
Nickel metal(Component of NIC 7440-02-0 0.23586 08 0 0.000034
Perchloroeth lene tetrachloroeth lene 127-18-4 0.00264 08 0. 3.8E-7 AFTER
Phenol 108-95-2 0.6937 08 0 0.0001 AFTER
Phosphorus Metal Yellow or White 7723-14-0 , 3.81535 08 0 0.00055 AFTER
Selenium Compounds SEC 0.32604 08 0 0.000047 AFTER
Styrene- 100-42-5 0.02914 08 0 0.0000042 AFTER
Toluene 108-88-3 2.98291 . 08 0 0.00043 AFTER
Vinyl acetate 108-05-4 0.00132 08 0 1.9E-7 AFTER
X lene 1330-20-7 0.25181 08 0 0.0000363 AFTER
X lene o- 95-47-6 0.05064 08 0 0.0000073 AFTER
21

I
Original COPY of RECORD Date Submitted: 6I27/2013 11 :51 :25
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 2012
1. Emission Source ID(from permit)or Group G-69 consisting of ES—CR5,ES—CR6,ES—CR7
Emission Source Group ID
2. Emission Source Description: Texturizing Operations
3. Operating Scenario ID/Description: OS—37/Texturizing Operations
t
4. SCC Number/Description: Not required by facility,will be completed by DAQ
5. Throughput/units in 2012: 87319 TON/yr
(e.g.production or fuel use):
6. Fuel Information (1f fuel is used) /° Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-19 CD—CR6BF ba filter 6,096 square feet of filter area
2 CS-19 CD—CR7BF 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
I
t
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional e try lines):
-_ ERP ID ERP Type Height Diameter Temperature Velocity) Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feettsec) Rate(Acfm)
_1Rectangle(L x W)
in 0.1 feet)
j EP—CR6 IHORIZONTAL STACKI 20 1 1 72 1 21.2 999.02 1ERP for ES—CR-6
EP—CR7 1HORIZONTAL STACKI 20 1 1 1 72 21.2 1 999.02 JEU for ES—CR-7
22

Operating Scenario: OS-37 Emission Source/Group ID: G-69
J10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2012)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
ran--Feb +Dec 250�o Farch-May 25% une-Aug. 25% Sept.-Nov. 25%
2 012 012
13. Actual Emissions per Pollutant Listed:
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions- Emission Control
GIiG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2012
Criteria Emissions Emission Control
Pollutant Criteria Estimation Efficiency Emission
��QS) Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2012
CO CO - 08
NOx NOx 08
_ TSP TSP 0.16 08 99
PM10 PM10 0.16 08 99
PM2.5 PM2.5 0.16 08 99
- S02 S02 08
VOC VOC 08
HAP/TAP CAS Emissions Emission
Estimation Control Emission
Pollutants (In (see instructions) HAP/TAPS Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
- 2012
23

Original COPY of RECORD Date Submitted: 6/27/201-3 11 :51 :25
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 2012
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
4. SCC Number/Description: 30500317/Brick Manufacture—Material Prep; Raw Material Unloading
5. Throughput/units in 2012: 430 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 100
Device or Stack):
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-10 CD—VS 1 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 RP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm) Description
ectangle(L x
1
in 0.1 feet)
EPVS2 DOWNWARD—FACING VENT 1 3 72 3.3 1400 ERP for
CD—VS2
ERP for
EPVS1 DOWNWARD—FACING VENT 1 3 72 3.3 1400 CD—VS1
J
24

J
Original COPY of RECORD Date Submitted: 6/27/2013 11 :51 :25
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 2012
1. Emission Source ID (from permit) or Group G-71 consisting of F—C—CFBH,F—FC4,F—FC5,F—FS 1,F—FS2,
Emission Source Group ID F—FS3,F—FS4,F-FS5,F—FS6,F—FS7,F—FS8,F—FS9,F-HM.12A,F—PC,
F—SS1,F—SS2
2. Emission Source Description: Clay Handling Equipment
3. Operating Scenario ID/Description: OS—3I/Primary Clay Grinding and Screening Operation
4. SCC Number/Description: 30500302/Brick Manufacture—Material Prep;Raw Material Grinding
Screening
5. Throughputtunits in 2012:, 106067 TON/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
Btu/units
I
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point RP Information: Sources vented to more than one ERP use additional entry lines
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
EP—FG TUGITWE(NO 1 72 Area= 1 ERP for Fugitive
— STACK) sources
26

' I
Operating Scenario: OS—34 Emission Source/Group ID: G-70
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2012)
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:
V
n—Feb +Dec o o une—Aug. o Sept.—Nov. o
12 25/0 �arch—May
12 25/0 012 25�O 012 25/o
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
(Tons/Year See Instructions all controls
2012
Criteria Emissions— Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission Ef Control
Pollutants Code Pollutants Method Code (Net after Factor
(Tons/Year) (See Instructions) all controls)
2012
CO CO 08 0
NOx NOx 08 0
TSP TSP 0.03 08 99.9
PM10 PM10 0.03 08 99.9
PM2.5 PM2.5 0.03 08 99.9
S02 S02 08 0
VOC VOC 08 0
HAP/TAP Emissions Emission Control
Pollutants (in CAS HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2012 -
25

Operating Scenario: OS—31 Emission Source/Group ID: G-71
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2012)
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 I 25% 25% une—Aug. 25%' Sept.—Nov. 25%
012 �arch-7May
12 �012 012
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
2012
r
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)
2012
CO CO 08
NOx- NOx 08
TSP TSP 1.38 08
_ PM10 PM10 0.15 08
PM2.5 PM2.5 0.13 08
S02 S02 08
v0C VOC 08
-- HAP/TAP CAS Emissions Emission Control
Pollutants (in HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code y Factor
Alphabetical,Order Pounds/Year
) ( ) (Net after all controls)
See Instructions
2012
I ,
27

Original COPY of RECORD Date Submitted: 6/27/2013 11 :51 :25
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 2012
1. Emission Source ID (from permit)or Group G-72 consisting of I—ES—K1D1, I—ES—K2D1
Emission Source Group ID
2. Emission Source Description: Dryers associated with materials handling equipment
3. Operating Scenario ID/Description: OS— 15/Dryers associated with Kilns 1 and 2
4. SCC Number/Description: 30500305/Brick Manufacture—Material Prep;Raw Material Handling and
Transferring
5. Throughput/units in 2012:
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) r-9
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—H) CD ID Control Device Description
as listed inpermit)
9.Emission Release Point RP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) (Acfm)
ectangle(L x W)
in 0.1 feet)
EP—FG FUGITIVE(NO 1 72 Area= 1 ERP for Fugitive
STACK) sources
28

Operating Scenario: OS— 15 Emission Source/Group ID: G-72
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2012)
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 hput:
' an—Feb +Dec� 25% arch—May 25% une—Aug. 25% �012
ept.—Nov. 25%
2012 �012 �012
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
" 2012
Criteria Emissions— Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency .Emission Ef Control
Pollutants Code Pollutants Method Code (Net after Factor
(Tons/Year) (See Instructions) all controls)
2012
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
Emission
HAP/TAP CAS Emissions Estimation Control Emission
Pollutants (In (see instructions) HAP/TAPS- Efficiency Factor EF Control
Method Code
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions)
2012
29

Original COPY of RECORD Date Submitted: 6/27/2013 11 :51 :25
As entered in AERO
Facility Name: General Shale Brick,Inc. Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit: 04384
7 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 2012
1. Emission Source ID (from permit)or Group G-135 consisting of ES—K4D1,ES—K4D2,ES—K4D3
Emission Source Group ID
2. Emission Source Description: Natural gas/propane—fired dryers at Brickhaven Plant
3. Operating Scenario ID/Description: OS—29/Natural gas/propane—fired dryers for Kiln 4
4. SCC Number/Description: 3050035l/Brick Manufacture—Dryer;Brick Dryer: Heated With Waste Heat
And Supplemental Gas Burners
i
5. Throughput/units in 2012: 80382 TON/yr
(e.g.production or fuel use):
i
6. Fuel Information (If fuel is used) ro
Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
J
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 Description
f (in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
EP—K4D1 VERTICAL STACK 34.78 4.92 99.95 33.79 38544.24 Brick KDryerson
I`
30

Operating Scenario: OS—29 Emission Source/Group ID: G-135
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2012)
J 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 25a�o une—Aug. 250�o �012
ept.—Nov. 25"�0
2012 �012 �012 i
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/Ye See Instructions all controls
2012
� Criteria
Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po� Code Pollutants Method Code (Net after. Factor Ef Control
Pollutants - -
i
(Tons/Year) (See Instructions) all controls)
2012
CO CO 11.25 08 0.28
NOx NOx 3.94 08 0.098
TSP TSP 7.52 08 0.187
PM10 PM10 7.52 08 0.187
PM2.5 PM2.5 7.52 08 0.187
S02 S02 08
VOC VOC 1.21 08 0.03
HAP/TAP CAS Emissions Emission Control
Pollutants (in HAP/TAPS Estimation Emission
(see instructions) Efficiency EF Control
Alphabetical Order Method Code Factor
p ) (Pounds/Year) See Instructions (Net after all controls)
- 2012
f
i
31

i
Original COPY of RECORD Date Submitted: 6/27/2013 11 :51 :25
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 2012
1. Emission Source ID(from permit)or Group G-144 consisting of IES—Tl,IES—T2,IES—T3,IES—T4,IES—T5
Emission Source Group ID
-- 2. Emission Source Description: Storage tanks
i
3. Operating Scenario ID/Description: OS.— 18/Storage tanks
4. SCC Number/Description: 39090004/Fuel Storage—Fixed Roof Tanks ;Distillate Oil(No. 2): Working
Loss
5. Throughput/units in 2012: 29300 GAL/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
_ Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
EP—FG FUGITIVE(NO 1 72 Area= 1 ERP for Fugitive
STACK) sources
V
32

Operating Scenario: OS— 18 Emission Source/Group ID: G-144
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2012)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 250�o 25% June—Aug. 25% �012
ept.—Nov. 25%
012 Varch—May
12 �2012
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
2012
Criteria Emissions— Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission Ef Control
Pollutants Code Pollutants Method Code (Net after Factor
(Tons/Year) (See Instructions) all controls)
2012
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 0.21 08
Emission
HAP/TAP Emissions 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
2012
F -
i
i
33

i
- Original COPY of RECORD Date Submitted: 6/27/2013 11 :51 :25
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 2012
1. Emission Source ID (from permit)or ES—BP—BM
Emission Source Group ID
2. Emission Source Description: batch mixer(39.97 tons per hour capacity)
3. Operating Scenario ID/Description: OS—26/Batch Mixer
4. SCC Number/Description: 31299999/Miscellaneous Machinery; Other Not Classified
5. Throughputlunits in 2012:
-' (e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content
to/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-12 CD—BP—BH1 one ba filter 535 s aure feet of filter area
9.Emission Release Point 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) (Feettsee) 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
i
i
i
34

i
Operating Scenario: OS—26 Emission Source/Group ID: ES—BP—BM
1 10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2012)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
ran--Feb +Dec arch—May une—Aug. Sept.—Nov.
25/ 25% 25/
12 0122 0
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 2012
Emissions— Emission Control
Criteria Pollutant Criteria Estimation Efficiency Emission
Po�QS Code Pollutants Method Code (Net after Factor Ef Control
Pollutantss
(Tons/Year) (See Instructions) all controls)
2012
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 , 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
Emission
HAP/TAP CAS Emissions Control
Estimation Emission
Pollutants (In (see instructions) HAP/TAPS Efficiency Factor EF Control
Method Code
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2012
R
35

Original COPY of RECORD Date Submitted: 6/27/2013 11 :51 :25
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 2012
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
I
5. Throughput/units in 2012:
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information :
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-13 CD—BP—BV2 one bin vent filter 227 square feet of filter area
_ i
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (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
36

Operating Scenario: OS—27 Emission Source/Group ID:ES—BP—CS
10.Operating Schedule: (Source/Operating Scenario that best.characterizes Calendar Year 2012)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
ran-Feb +'Dec 25% arch—May 25% une-Aug. 25% Sept.—Nov. 25%
012 012 012 012
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
2012
i
Criteria Emissions— Emission Control
_ Pollutant Criteria Estimation Efficiency Emission
��QS) Ef Control
Code Pollutants Method Code (Net after Factor
Pollutants
(Tons/Year) (See Instructions) all controls)
2012
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP Emissions Emission Control
Pollutants (in CAS HAP/TAPS Estimation Efficiency .Emission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) See Instructions) (Net after all controls)
2012
37

i
Original COPY of RECORD Date Submitted: 6/27/2013 11 :51 :25
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 2012
I 1. Emission Source ID (from permit)or ES—BP—FAS
Emission Source Group ID
2. Emission Source Description: flyash silo(11 tons per hour capacity)
i
3. Operating Scenario ID/Description: OS—28/Flyash Silo
4. SCC Number/Description: 31299999/Miscellaneous Machinery Other Not Classified
5. Throughput/units in 2012:
(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 inpen-nit)
1 CS-14 CD—BP—BH1 one ba filter 535 s aure feet of filter area
I
9.Emission Release Point RP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feettsec) Rate(Acfm)
tRectangle(L x W)
in 0.1 feet)
FLY VERTICAL STACK 44.95 1.15 72 60 3739.28 Flyash Silo Bin
Vent
38

Operating Scenario: OS—28 Emission Source/Group ID: ES—BP—FAS
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2012)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
ran�--Feb .+Dec 250�o Farch—May 25% tine—Aug. 25%' Sept.—Nov. 25%
2 012 012
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) ctions) all controls
2012
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
o�QS Code Pollutants Method Code (Net after Factor Ef Control
Pollutantss
(Tons/Year) (See Instructions) all controls)
2012
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
Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
r
See Instructions
2012
39

I
Original COPY of RECORD Date Submitted: 6/27/2013 11 :51 :25
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 2012
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 maximum
heat input; 3.45 tons per hour capacity)
3. Operating Scenario ID/Description: OS—6/Rotary sand drum dryer(3.45 tons per hour)
4. SCC Number/Description: 30500301/Brick Manufacture—Dryer; Raw Material Drying
z 5. Throughput/units in 2012:1 0.098 E6FT3/yr
(e.g.production or'fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate EPP Description
(in feet) Circle(enter ft (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
F
P—FG FUGITIVE(NO 1 72 Area= 1 ERP for Fugitive
STACK) sources
i
40

Operating Scenario: OS—6 Emission Source/Group ID: ES—CD-8
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2012)
Hours per Day ( 24 ) Days per Week .( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating'Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec o arch—May o une—Aug. o Sept.—Nov.. o
012 25/0 012 25/0 012 25/0 012 25/o
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2012
r Emissions— Emission Control
Criteria Pollutant Criteria Estimation Efficiency Emission
(NAAQS) Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2012
CO CO 08
NOx NOx 08
TSP TSP 0.03 08
PM10 PM10 0.03 08
PM2.5 PM2.5 0.03 08
S02 S02 08
VOC VOC 08
Emissions Emission Control
HAP/TAP CAS Estimation Efficiency Emission
Pollutants (In Alphabetical Order) (see instructions) HAP/TAPS(Pounds/Year) Method Code (Net after all Factor EF Control
-
See Instructions controls)
2012
Benzene 71-43-2 0.00021 08 0.0021
Formaldehyde 50-00-0 0.00735 08 0.075
- Hexane,n— 110-54-3 0.1764 08 1.8
Naphthalene(Component of 91-20-3 0.00006 08 0.00061
POMT
Toluene 108-88-3 0.00033 08 0.0034
41

Original COPY of RECORD Date Submitted: 6/27/2013 11 :51 :25
As entered i-n 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 2012
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 2012: 3253 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):
f -
8. Control Device Information :
Order CS—II) CD ID Control-Device Description
as listed inpermit)
1 CS-18 CD—Coal—CC ba filter air to cloth ration of 4.7 to 1
I
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height iameter Temperature Velocity Volume Flow ERP Description
.(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
ectangle(L x W)
(in 0.1 feet)
P—Coal—CC VERTICAL STACK 30 2 75 18.56 3500 One Bagfilter
_I
42

Operating Scenario: OS—33 Emission Source/Group ID: ES—Coal—CC
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2012)
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%
2012 012 012 012
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
2012
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po�QS Code Pollutants Method Code (Net after Factor Ef Control
Pollutantss (Tons/Year) (See Instructions) all controls)
2012
CO CO 08 0
NOx NOx 08 0
TSP TSP 0.02 08 99 1.1 BEFORE
PM10 PM10. 0.02 08 99 1.1 BEFORE
PM2.5 PM2.5 0.02 08 99 1.1 BEFORE
S02 S02 08 0
VOC VOC 08 0
HAP/TAP Emissions Emission Control
Pollutants (in CAS HAP/TAPS Estimation Efficient Emission EF Control
(see instructions) Method Code y Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions)
2012
43

Original COPY of RECORD Date Submitted: 6/27/2013 11 :51 :25
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 2012
1. Emission Source ID (from permit)or ES—K3K
Emission Source Group ID
2. Emission Source Description: Coal/natural gas/propane—fired brick tunnel kiln(25.9 million Btu per hour
maximum heat input and 20.55 tons per hour maximum fired brick production-
_ " rate) [Case By Case MACT]
3. Operating Scenario ID/Description: OS — 10/Natural gas/propane—fired kiln#3 (Uncontrolled).
4. SCC Number/Description: 30500311/Brick Manufacture—Curing Firing;Curing and Firing: Gas—fired
Tunnel Kilns
5. Throughput/units in 2012:
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
'7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None `
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
ERP for ES—K3K,
EP—K3 VERTICAL STACK 35 4.92 99.95 33.79 38544.24 ES—K3D1 AND
ES—K3D2
44

Operating Scenario: OS— 10 Emission Source/Group ID: ES—K3K
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2012)
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"�u une—Aug. 25% Sept.—Nov. 25%
2012 012 012 012
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
2012
Criteria Emissions— Emission Control
NAAQS Pollutant Criteria Estimation Efficiency Emission Ef Control
Pollutants Code Pollutants Method Code (Net after Factor
(Tons/Year) (See Instructions) all controls)
2012
CO CO 08
NOx NOx 08-
_ TSP TSP 08
PM10 PM10 08
i PM2.5 PM2.5 08
S02 S02 08
- - VOC VOC 08
HAP/TAP rEmissions Emission Control
CAS Estimation Emission
Pollutants (In (see instructions) HAP/TAPS Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2012
i
45

Original COPY of RECORD Date Submitted: 6/27/2013 11 :51 :25
As entered in AERO
Facility Name: General Shale Brick,Inc.Moncure Facility Facility ID : 1900009
T 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 2012
1. Emission Source ID (from permit)or ES—K3K
Emission Source Group ID
2.- Emission Source Description: Coal/natural gas/propane—fired brick tunnel kiln(25.9 million Btu per hour
maximum heat input and 20.55 tons per hour maximum fired brick production
rate)[Case By Case MACT]
3. Operating Scenario ID/Description: OS—25/10/Natural gas/propane/coal—fired kiln#3
4. SCC Number/Description: 30500311/Brick Manufacture—Curing Firing;Curing and Firing: Gas—fired
Tunnel Kilns
5. Throughput/units in 2012:
-(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /° Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-15 CD—K3DLA dry limestone adsorber
9.Emission Release Point 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)
F
—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 2012)
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:
F
Feb +Dec 25% arch—May 25% une—Aug. 25% �012
ept.—Nov. 25%
012 012
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
2012
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po� Code Pollutants Method Code (Net after Factor Ef Control
Pollutants (Tons/Year) (See Instructions) all controls)
2012
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
Emissions Emission Control
HAP/TAP CAS Estimation Emission
Pollutants (In (see instructions) HAP/TAPS Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) See Instructions) (Net after all controls)
2012
I
1
ti
47

Original COPY of RECORD Date Submitted: 6/27/2013 11 :51 :25
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 2012
1. Emission Source ID(from permit)or ES—K4K
Emission Source Group ID
2. Emission Source Description: Coal/natural gas/propane—fired brick tunnel kiln(25.9 million Btu per hour
maximum heat input and 20.55 tons per hour maximum fired brick production
rate) [Case By Case MALT]
3. Operating Scenario ID/Description: OS—2 1/Coal/Natural gas/Propane—fired kiln#4
4. SCC Number/Description: 30500311/Brick Manufacture—Curing Firing;Curing and Firing: Gas—fired
Tunnel Kilns
5. Throughputtunits in 2012: 80382 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
I
9.Emission Release Point RP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
P—K4DLA VERTICAL STACK 75.13 4.92 469 43.64 49780.13 Dry limestone
M adsorber on Kiln 4.
48

Operating Scenario: OS—21 Emission Source/Group ID: ES—K4K
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2012)
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:
roran--Feb +Dec 250�o arch—May 25"�o une—Aug. 25% Sept.—Nov. 25%
2 012 012 012
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emission
Emissions— Estimation Control
GHG CAS GHG Method Efficiency Emission Ef Control
Pollutants. Pollutants Code (Net after. Factor
7 (Tons/Year) (See all controls)
i
` Instructions
2012
I J
Emission
Criteria Emissions— Estimation Control
Pollutant Criteria Method Efficiency Emission
-- �� Code Pollutants Code (Net after `Factor Ef Control
Pollutants
(Tons/Year) (See all controls)
Instructions
2012
CO CO 32.6 08 0
NOx NOx 32.7 08 0
TSP TSP 40.3 08 0
-- PM10 PM10 31.9 08 0
PM2.5 PM2.5 31.9 08 0
S02 S02 62.3 08 0
VOC VOC 0.97 08 0
Emission
Emissions Estimation Control
-- HAP/TAP CAS Emission
HAP/TAPS Method Efficiency EF Control
Pollutants (In Alphabetical Order) (see instructions) Code (Net after all Factor
(Pounds/Year)
(See controls)
Instructions
2012
Antimony Unlisted Compounds(Specify SBC—Other 2.17031 08 0 0.000027 AFTER
Component of SBC
Arsenic Unlisted Compounds(Specify
Component of ASC ASC—Other 7.27 08 0
Benzene 71-43-2 107 08 0
Beryllium metal(unreacted) 7440-41-7 0.785 08 0
(Component of BEC
CFC-11 richlorofluoromethane 75-69-4 1.13 08 0
Cadmium Metal(elemental unreacted, 7440-43-9 1.20573 08 0 0.000015 AFTER
Component of CDC
49

-_, Carbon disulfide 75-15-0 1.49 08 0
- Carbon tetrachloride 56-23-5 0.00804 08 0
Chlorine 7782-50-5 104.4966 08 0 0.0013 AFTER
Chloroform 67-66-3 0.00804 08 0
Chromic acid(VI)(Component of 7738-94-5 4.09948 08 0 0.000051 AFTER
SolCR6 CRC
Cobalt Unlisted Compound(Specify COC-Other 0.1688 08 0 0.0000021 AFTER
Component of COC
Di 2-eth lhex 1 hthalate EHP) 117-81-7 67.8 08 0
Dibu 1 hthalate 84-74-2 11.25348 08 0 0.00014 AFTER
Dichlorobenzene , 14- 106-46-7 1.7 08 0
Dimeth I phthalate 131-11-3 0.0627 08 0
Eth l benzene 100-41-4 2.43 08 0
Ethyl chloride chloroethane 75-00-3 18.9 08 0
Fluorides(sum of all fluoride 16984-48-8 4900 08 0
compounds
Formaldehyde 50-00-0 0.0019 08 0
Hydrogen chloride(hydrochloric acid 7647-01-0 4678.5 08 0 AFTER
Hydrogen fluoride(hydrofluoric acid as 7664-39-3 3065.2 08 90 AFTER
j mass of HF-Component of Fluorides
Lead Unlisted Compounds(Specify and PBC-Other 12.0573 08 0 0.00015 AFTER
Component of PBC
j Manganese Unlisted Compounds MNC-Other 23.31078 08 0 0.00029 AFTER
(Specify Component of MNC
Mercury,vapor(Component of HGC 7439-97-6 4.87 08 0
r
Methyl bromide 74-83-9 1.92917 08 0 0.000024 AFTER
Methyl chloride 74-87-3 26.8 08 0 AFTER
Methyl chloroform 71-55-6 0.971 08 0 AFTER
Methyl ethyl ketone 78-93-3 19.1 08 0
Methyl iodide 74-88-4 7.47553 08 0 0.000093 AFTER
Methylene chloride 75-09-2 0.0643 08 0
Naphthalene(Component of POMT 91-20-3 2.42 08 0
Nickel metal(Component of NIC 7440-02-0 5.7875 08 0 0.000072 AFTER
Perchloroeth lene tetrachloroeth lene 127-18-4 0.22507 08 0 0.0000028 AFTER
Phenol 108-95-2 4.45 08 0
Phosphorus Metal,Yellow or White 7723-14-0 78.8 08 0
Selenium Compounds SEC 18.48786 08 0 0.00023 AFTER
Styrene 100-42-5 0.648 08 0
Toluene 108-88-3 17.2 08 0
Vinyl acetate 108-05-4 0.00804 08 0 lE-7 AFTER
X lene 1330-20-7 12.6 08 0
Xylene,o- 95-47-6 4.13 08 0
i 50

Original COPY of RECORD Date Submitted: 6/27/2013 .11 :51 :25
- 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 2012
-1. Emission Source ID(from permit)or ES—RUMBLE
Emission Source Group ID
2. Emission Source Description: rumbler system
i
- 3. Operating Scenario ID/Description: OS—36/Rumbler tumbles blocks in a rotating drum in order to create an
4. SCC Number/Description: 30500397/Brick Manufacture; *Other Not Classified
5. Throughput/units in 2012:
(e.g.production or fuel_use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
- 7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information:None
Order CS—ID CD ID Control Device Description
'i as listed inpermit)
9.Emission Release Point RP Information: Sources vented to more than one ERP use additional entry lines)-
ERP ED 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)
-- VP-RUMBLE VERTICAL STACKI 44.95 1.312 72.05 40.02 3246.27 Rumbler Ba house
l
rl
51

i �
Operating Scenario: OS—36 Emission Source/Group ID:
ES—RUMBLE
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2012)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
ran-'—Feb +Dec May une—Aug. Sept.—Nov.250�0 012 25% 25% 25%0122
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
2012
Criteria Emissions— Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission Ef Control
Pollutants Code Pollutants Method Code (Net after Factor
(Tons/Year) (See Instructions) all controls)
2012
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
CAS Estimation
(see instructions) Method Code Control Emission
Pollutants (In HAP/TAPS Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2012
G
I
52

Original COPY of RECORD Date Submitted: 6/27/2013 11 :51 :25
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 2012
1. Emission Source ID(from permit)or IS-14
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: 30500397/Brick Manufacture; *Other Not Classified
5. Throughput/units in 2012:
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur/Ash Heat Content
(Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8, Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
I 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) (Feettsec) (Acfm)
Rectangle(L x W)
j (in 0.1 feet)
EP—FG FUGITIVE(NO 1 72 Area= 1 ERP for Fugitive
STACK) sources
I -
I �
53

Operating Scenario: OS— 19 Emission Source/Group ID: IS-14
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2012)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
r01an--Feb2
+Dec 25% arch—May 25% une—Aug. 25% Sept.Nov. 25%
012 012 012
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
2012
Criteria Emissions— Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission Ef Control
Pollutants . Code Pollutants Method Code (Net after Factor
(Tons/Year) (See Instructions) all controls)
2012
CO CO 08
I
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP Emissions Emission Control
Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Factor
Alphabetical Order) (Pounds/Year) Method Code (Net after all controls)
See Instructions
2012
i
I
54

i
Facility Total CY 2012 Emissions Summary
_J Original COPY of RECORD Date Submitted: 6/27/2013 11 :51 :25
j
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 2012
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 2012 2011 %Difference
Criteria Pollutants
Actual Emissions Tons/Year
Pollutant CAS 2012 2011 %Difference
CO -CO 45.04 76.05 —40.775806%
NOx NOx 37.92 26.32 44.072945%
PM TSP TSP 51.94 76.27 —31.899828%
PM 10 PM 10 42.31 44.63 —5.198296%
i
PM2.5 PM2.5 42.29 .8 5186.25%
S02 S02 62.94 47.77 31.756327%
VOC V0C 3.01 5.72 —47.377617%
' Hazardous Air Pollutants HAPS and/or Toxic Air Pollutants TAPS
Actual Emissions(Pounds/Year)
Pollutant CAS 2012 1 2011 1 %Difference
Pollutant Group:Antimony Co m ounds total mass,inc elemental SB Group Sum.2.18973
Antimony Unlisted Compounds(Specify SBC—Other 2.18973 1.9953 9.744392%
i Component of SBC) L
Pollutant Group:Arsenic Compounds(total mass of elemental AS,arsine and all inorganic compounds) Group
Sum:7.41568
Arsenic Unlisted Compounds(Specify ASC—Other 7.41568 7.14448 3.7959332%
Component of ASC
Pollutant Group:13eryllium compounds Total mass Group Sum:.78715
Beryllium metal(unreacted)(Component o BEC 7440-41-7 0.78715 .69435 13.365022%
f
Pollutant Grou :Cadmium compounds total mass inc elemental metal GroupSum:1.35834
Cadmium Metal(elemental unreacted
Component of CDC 7440-43-9 1.35834 1.91979 T-29.245386%
Pollutant Grou :Cobalt compounds Group Sum%1688
Cobalt Unlisted Compound(Specify COC—Other 0.1688 .14655 15.182529%
55 .

- Component of COC
Pollutant Grou :Lead and Lead com ounds roup Sum:12.88974
Lead Unlisted Compounds (Specify and PBC-Other 12.88974 15.23093 -15.371289%
Component of PBC
Pollutant Grou :Man anese compounds roup Sum:26.64054
Manganese Unlisted Compounds(Specify MNC-Other 26.64054 39.39958 -32.383694%
Component of MNC
Pollutant Grou :Mercu Compounds-all total mass, inc Hg Vapor Group Sum:4.94631
Mercury,vapor(Component of HGC 7439-97-6 4.94631 4.66649 5.996369%
ollutant Grou :Nickel Compounds,sum total mass,inc elemental Group Sum:6.02336
Nickel metal(Component of NIC 7440 02-0 6.02336 6.54417 -7.9583836%
Pollutant Grou :Chromium VI Soluble Chromate Com ounds(Component of CRC) roup Sum:4.43246
Chromic acid(VI)(Component of So1CR6 7738-94-5 4.43246 5.46942 -18.959234%
CRC
Pollutant Grou :Chromium-All/Total Inc Chromium VI categories,metal and Others Group Sum:4.43246,
Chromic acid(VI)(Component of So1CR6 7
CRC 738-94-5 4.43246 5.46942 -18.959234%
Pollutant Grou :Pol c clic Organic Matter(Specific Compounds from OA PS for TV Group Sum:2.42008
Naphthalene(Component of POMTV 91-20-3 2.42008 2.10016 15.233129%
Acrylonitrile 107-13-1 0.1318 .75394 -82.51851%
Benzene 71-43-2 110.88493 115.32157 -3.8471882%
CFC-II Trichlorofluoromethane 75-69-4 1.13694 1.01668 11.828697%
Carbon disulfide 75-15-0 1.61487 2.01426 -19.82813%
Carbon tetrachloride 56-23-5 0.01068 .02206 -51.58658%
Chlorine 7782-50-5 104.4966 90.7205 15.185212%
Chloroform 67-66-3 0.01068 .02206 -51.58658%
Di 2-eth lhex 1 hthalate DEHP 117-81-7 68.77118 64.45534 6.6958637%
Dibu 1 hthalate 84-74-2- 11.36447 10.4048 9.2233305%
Dichlorobenzene , 1,4- 106-46-7 1.7 1.47 15.646259%
Dimeth 1 phthalate 131-11-3 0.06272 .0545 15.082573%
Ethyl benzene 100-41-4 2.49937 2.50681 -0.29678562%
Ethyl chloride chloroethane 75-00-3 18.9 16.4 15.243903%
Fluorides sum of all fluoride compounds) 16984-48-8 6772.99 18862.608 -64.09303%
Formaldehyde 50-00-0 17.97925 88.80925 -79.7552%
Hexane,n- 110-54-3 0.1764 .1764. 0.0%
Hydrogen chloride(hydrochloric acid 7647-01-0 5857.79 10805.77 -45.79016%
Hydrogen fluoride(hydrofluoric acid as °
-' mass of HF-Component of Fluorides 7664-39-3 4660.71 11796.63 -60.457653/°
Methyl bromide 74-83-9 2.2344 3.4208 -34.681942%
Methyl chloride 74-87-3 36.5118 78.8534 -53.69661%
Methyl chloroform 71-55-6 0.97461 .86363 12.850408%
Methyl ethyl ketone 78-93-3 20.62614 25.32982 -18.569733%
Methyl iodide 74-88-4 9.14041 16.01345 -42.920418%
Methylene chloride 75-09-2 0.49439 2.51602 -80:35032%
Perchloroeth lene tetrachloroeth lene 127-18-4 0.22771 .21048 8.186046%
Phenol 108-95-2 5.1437 7.8381 -34.375675%
Phosphorus Metal,Yellow or White 7723-14-0 82.61535 90.26297 -8.472601%
Selenium Compounds SEC 18.8139 1 17.9156 5.014067%
Styrene 100-42-5 -J-0.67714 .72866 -7.070512%
56

li
Toluene 108-88-3 20.18324 31.96316 —36.854675%
- , Vinyl acetate 108-05-4 0.00936 .01452 —35.537193%
X lene 1330-20-7 12.85181 12.34042 4.14403%
X lene,o— 95-47-6 4.18064 3.87967 7.7576265%
57

Original COPY of RECORD Date Submitted: 6/27/2013 11 :51 :25
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:
6/25/2013—Emission Group Comments
EUG G-69 : This emission group should also contain ES—CR8 but it cannot be grouped in G-69 because its emission group
description and source type are different from the other sources grouped in G-69.Therefore,emissions from ES—CR8 are
included in G-69,even though it was marked as not required to be reported in AERO.
58

SECTION 2
2012 SUPPORTING EMISSION CALCULATIONS
General Shale Brick, Inc. -Moncure, NC Facility I CY 2012 Emissions Inventory
Trinity Consultants

Title: 2012 Air Emission Inventory
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
Critical Parameters Table
Parameter I Value
Combustion Sources-Ca a Fear_
Actual Brick Production 1 6,937 tons per year
Actual Sawdust Usage 2,71() tpy
� Go%bdeE p;$oar<es�$dckhayen-Kiln 3 and Associated Dryers
Actual Brick Production(Natural Gas) 0 tPy
Actual Brick Production(Coal&NG) 0 tPy
Actual Gas Usage 0 scf/yr
Actual Coal Usage 0 tPy
Combustion Sources-Brickhaven-Kiln 4 and Associated Dryers
Actual Brick Production(Natural Gas) 0 tPy
Actual Brick Production(Coal&NG) 80,382 tpy
Acutal Gas Usage 91,709,702 scf/
Actual Coal Usage 3,253 t
"'Wood WasteSystem-Cape Fear 4
Number of Cyclones I I
Sawdust preparation I0 i hr/vr
Clay Handling Operations
Actual Raw Material Processed 106,067 tpy
Hours ofoperations 1,440 hr/yr
Intersite Conveyor x
Process Throughput 97,234 tpy
Sand Dryer-Ca a Fear ",,
Hours of operations 400 hr/yr
jYrjX'W turring O erations �W -`'
Actual Brick Production 80,382 tpy
Baghouse Efficiency 99.8%
Hours of operation-Brick Haven 2,080 hr/yr
Hours of o rations-Cape Fear 160 hr/yr
<'Vacuum systems
Hours of o erations-Cape Fear(VS1) 160 hr/yr
Hours of o erations-Brick Haven VS2 270 hr/yr
Hours of operations-Brick Haven VS3 -Kiln 3 1,920 hr/yr
Hours of operations-Brick Haven VS4&VSS 0 hr/yr
Fl ash�ilii r�
FI ash silo'l hrou h ut 0 tPY
_''.Cement Sil
Cement silo Throughput 0 tPY
Mixer Loading
Mixer Loading Throughput 0 tPY
Aggregate Loading
Aggregate Loading Throughput 0 tPY
Rumbler
Hours of operations 0 hr/ r
Fuel Usage
Diesel Tank 20,000gal/yr
Gasoline Tank 1,200gal/yr
Waste Oil Tank 200gal/yr
Motor Oil Tank 250gal/yr
Brick Oil Tank 2,500gal/yr
Gear Oil Tank 150gal/yr
Reference:
Information Provided by Warren Paschal,General Shale Brick,Inc.,June 2012
Support Calculations File: El 2012-Moncure.xlsx
Printed:6/27/2013 Page 1 of 35 Sheet: Input

I
Title: 2012 Air Emission Inventory
Source ID 0: ES-KI,ES-K2,ES-SDI
Facility: General Shale Brick,Inc.
Location: Moncure,NC -
Facility ID 0 1900009
Brick Processing System-Cape Fear
Description: After the wet clay is formed and coated it passes through the brick dryer and the kiln. The kiln`is
sawdust fired. Combustion products and heat generated by the kiln are vented to the drum dryer
which dries the sawdust. From the drum dryer the exhaust is vented to the atmosphere. However,not
all of the heat from the kiln is vented to the wood dryer. Instead,some evaporative heat is routed to
the brick dryers and vented to atmosphere.
Approach: The AP42 Section 11.3 is used to estimate the emissions from these emission units, except for
fluoride and hydrogen fluoride factors developed from a GSB test at Monctue.
Parameter Value
Actual Brick Production 6,937 tpy
Actual Sawdust Usage 2,710 tpy
EMISSION CALCULATIONS
Emissions are calculated by the following equation:
Yearly Emissions -
Emission Factor(lb/tons brick) Brick Production(tpy)=Emissions(lb/yr) -
Emissions(16/yr)/2000 lb/ton=Emissions(tpy)
-- Note:The Formaldehyde emissions are multiplied by the wood usage instead of bricks usage.
I
Support Celculatlons File:EI2o12-Monwrejdsx
Printed:=712013 Page 2 of 35 Street:Brick-CF(G-66)

05- 14
_ Source: ES-Kl,ES-K2,ES-SDI Sawdust Kilns 1&2 and sawdust dryer
Actual Annual Process Throughput: 6,937 Tons/yr
Brick Kiln Fuel: Wood
Annual Annual
TAP NO. CAS NO. Emission Factor°(lb/ton Emission Rate Emission Rate
Pollutant fired bricks produced) (lbs/yr) (TPY)
PM 0.675 Id `V 1.4' ? 4,66 -jLPy
PM-10 0.675 Id gyp,31 A
_ PM 2.5 0.675 7d y,682
S02 -0--64, a.32y
NOx 0.37 Iad 2,567 1.28
VOC 0.18 �" 1,249 0.62
CO 0.344 d {.!o. -1-4� 5i 55 spy
1,4-dichlorobenzene 36 106-46-7 0.00E+00 0.00E+00
2-butanone(MEK) 70 78-93-3 2.20E-04 a6 1.53E+00 7.63E-04
2-mcthylphenol(cresol) 35 9548-7 2.40E-09 jab 1.66E-05 8.32E-09
Acrylonitrile 4 107-13-1 1.90E-05 lab 1.32E-01 6.59E-05
Antimony HAP A_NTIMONYCPDS 2.80E-06 h 1.94E-02 9.71E-06
t
Arsenic 9 ARSENICCPDS 2.10E-05 laa 1.46E-01 7.28E-05
Benzene 12 7143-2 5.60E-04 lab 3.88E+00 1.94E-03
Beryllium 16 BERYLCPDS 3.10E-07 l� 2.15E-03 1.08E-06
Bis(2-etbylhexyl)phthalate;di(2-
ethylhexyl)phthalate 39 117-87-7 1.40E-04 ab 9.71E-01 4.86E-04
Bromomcthane(Methyl Bromide) HAP 74-83-9 4.40E-05 Jab 3.05E-01 1.53E-04
Cadmium 23 CADMHIMCPDS 2.20E-05 l� 1.53E-01 7.63E-05
Carbon Disulfide 27 75-15-0 1.80E-05 lab 1.25E-01 6.24E-05
Carbon tetrachloride 28 56-23-5 3.80E-07 jab 2.64E-03 1.32E-06
Chlorine 29 0.00E+00 0.00E+00
Chooroethane(Ethyl Choroethane) HAP 1 75-00-3 0.00E+00 0.00E+00
Chloroform 31 67-66-3 3.80E-07 ab 2.64E-03 1.32E-06
Chloromethane(Methlyl Chloride) HAP 74-87-3 0.0014 ab 9.71E+00 4.86E-03
Chromium(expressed as chromic
acid) HAP CROMCPDS 4.80E-05 as 3.33E-01 1.66E-04
b
Cobalt HAP 7440484 j 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 Jb 1.66E-05 8.32E-09
Di-n-butylphthalate HAP 84-74-2 1.60E-05 lab 1.11E-01 5.55E-05
Ethylbenzene HAP 100-414 1.00E-05 lab 6.94E-02 3.47E-05
Fluorine 50 0.00E+00 0.00E+00
Formaldehyde 51 50-00-0 6.63E-03 ` 17.97 8.98E-03
Hydrazine HAP 0.00E+00 0.00E+00
Hydrogen Fluoride 59 7664-39-3 0.23 lb 1,595.51 7.98E-01
HCl 57 7647-01-0 0.17 ar 1,179.29 5.90E-01
Hydrogen Sulfide 60 7783-06-4 0.00E+00 0.00E+00
Iodomethane(Methyl Iodide) HAP 74-88-4 2.40E-04 d, 1.66E+00 8.32E-04
Lead HAP LEADCPDS 1.20E-04 (aa 8.32E-01 4.16E-04
M-/p-Xylene HAP 108-38-3/106-42-3 2.90E 05 ab 2.01E-01 1.01E-04
Manganese 62 MANGCPDS 4.80E-04 jaa 3.33E+00 1.66E-03
I I I-Trichloroethane
_ (methylchloroform) 68 71-55-6 5.20E-07 ab 3.61E-03 1.80E-06
Methylene Chloride 69 74-87-3 6.20E-05 lab 4.30E-01 2.15E-04
Mercury 66 MERCCPDS 1.10E-05 as 7.63E-02 3.82E-05
Naphthalene HAP 91-20-3 2.40E-09 lab 1.66E-05 8.32E-09
Nickel 75 NICKCPDS 3.40E-05 laa 2.36E-01 1.18E-04
o-Xylene HAP 9547-6 7.30E-06 lab 5.06E-02 2.53E-05
Ozone 0.00E+00 0.00E+00
Perchloroethylene
(Tetrachloroethene) 81 127-184 3.80F,07 lab 2.64E-03 1.32E-06
Phenol 82 108-95-2 1.00E-04 l'b 6.94E-01 3.47E-04
Phosphine 71 l 0.00E+00 0.00E+00
Phosphorus HAP 7723-14-0 5.50E-04 laa 3.82E+00 1.91E-03
Support Calculations File:E12012-kloncure.d=
Printed:er27/2013 Page 3 of 35 Sheet Brick-CF(GOa)

I
I
_ Selenium
_ HAP SEC 4.70E-05 la' 3.26E-01 1.63E-04
Styrene 91 10042-5 4.20E-06 i'b 2.91E-02 1.46E-05
Toluene 97 108-88-3 4.30E-04 lab 2.98E+00 1.49E-03
Total Fluorides(including HF) 50 16984-48-8 J)-2 1b O,its —W219 9 9-M— ZSa 2.8
Trichlorofluoromethane 100 75-694 1.00E-06 I'b 6.94E-03 3.47E-06
Vinyl acetate HAP 108-054 1.90E-07 lab 1.32E-03 6.59E-07
Xylene 104 1330-20-7 3.63E-05 12.52E-01 1.26E-04
Emission factors from AP42,Section 11.3,8/97
Table 11.3-7 for sawdust fired kilns and sawdust dryer.
ab Table 11.3-6 for sawdust fired kilns and sawdust dryer.
d0 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.
'f Table 11.3-4 for uncontrolled sawdust or natural gas fired tunnel kiln.
I
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)
c r
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= 2,710 tpy
d Testing was performed on Kiln 1 and Kiln 2 in June 2006.Emission Factors are as follows:
�= Process weight rate during test for both kilns 22.3 ton/hr
Highest Emissions Rate Emission
/ Pollutant Tested(lb/hr) Factor(lb/ton)
PM 15.05 0.675
CO 7.68 0.344
f�s'�'•�GC�I``�U 'o p�o 4°fyl�r/�yPC'j/J
�`�"^ ✓ ,,f �'r� � S02 data was from a September 27,2004 engineering test on Kiln 3 with *,tr
a process weight rate of` 19.58 tons/hr
Highest.Run Emissions Emission
Pollutant Rate.Tested(lb/hr)' Factor(Ib/ton)
S02 0.56 0.029
S02 factor for wood combustion AP-42-Section 1.6 0.025 lb/MMBm
MMBtu for wood=Tons wood fired*2000 Ib/ton'8000 Btu/lb
MMBtu for wood= 43,360 MMBtu
S02 Emissions=Tested lb/ton•Actual Production ton/yr+Wood Combustion Factor lb/Mmbtu MMBtuyr feed
S02 Emissions= 1,282 lbs(yr
�-14-���
/%) -Va®4 �i�. �/car "9R—4 -
Per
E017 ® X E,,I" V6;- W0'
I
I
Printed:B127l2013 Support Calculations Poe:EI2012-Moncure.du
Page 4 of 35 Sheet: Brick-CF(G-66)

Title: 2012 Air Emission Inventory
Source ID#: ES-K3K
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
i
Brick Processing System-Brick Haven-Kiln 3
Source: ES-K3K Kiln 3
Actual Brick Production: 0 Tonstyr
Coal Fired 0 Tonslyr
Brick Kiln Fuel: CoalING
60% Coal
40% Natural Gas
Control Eff.of HF 90% (NESHAP Requirement)
Uncontrolled Uncontrolled
Emission
TAP NO. Factor for Coal mission Ref Factor for i Tested Total
Natural Gas Emission Annual Annual.
Pollutant from AP42 from AP42 Ref Factors Ref Emissions Emissions
(lb/ton) (lb/ton) I I (lb/ton) . (1b/yr) (ton/ r)
PM 4.12E-01 g 0.00 0.00E+00
PM-10 2.03E-01 g 0.00 0.00E+00
PM-2.5 2.03E-01 g 0.00 0.00E+00
S02 38.000 f 2.86E-02 d 0.00 0.00E+00
NOx 8.13E-01. 0.00 0.00E+00
VOC 2.40E-02 ad 2.40E-02 ad 0.00 0.00E+00
CO 8.00E-01 ab 0.83 a; 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
111-Trichloroethane 68 1.70E-05 4.70E-06 of 0.00E+00 0.00E+00
(methylchloroform)
Methylene Chloride 69 8.00E-07 a` 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 a` 0.00E+00 0.00E+00
1,4-dichlorobenzene 36 3.20E-06 a` 4.80E-05 0.00E+00 0.00E+00'
-_ 2-butanone(MEK) 70 2.50E-04 a` 2.20E-04 of 0.00E+00 0.00E+00
2-Hexanone NA 9.40E-07 ae 8.50E-05 of 0.00E+00 0.00E+00
2-methylphenol(cresol) 35 2.20E-06 a` 0.00E+00 0.00E+00
2-methylnaphthalene NA 1.70E-06 a` 5.70E-05 of 0.00E+00 0.00E+00
Antimony NA 2.70E-05 ah 0.00E+00 0.00E+00
Acetone NA 6.80E-04 a` 1.70E-03 of 0.00E+00 0.00E+00
Arsenic 9 1.30E-04 ag 3.10E-05 ah 0.00E+00 0.00E+00
Benzene 12 2.90E-04 a` 2.90E-03 ae 0.00E+00 0.00E+00
Benzoic Acid 2.50E-04 a` 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 a` 2.00E-03 of 0.00E+00 0.00E+00
ethylhexyl)phthalate
Bromomethane(Methyl HAP 2.40E-05 ae 0.00E+00 0.00E+00
Butylbenzylphthalate NA 1.20E-06 a` 1.80E-05 of 0.00E+00 0.00E+00
Cadmium 23 1.50E-05 ah 0.00E+00 0.00E+00
Carbon Disulfide 27 2.30E-06 a` 4.30E-05 of 0.00E+00 0.00E+00
Support Calculations File: El 2012-Monare.)lSx
Printed:6/27/2013 Page 5 of 35 Sheet Brick-BH(ES-K3K G12)NG&Coal

I
Carbon tetrachloride 28 1.00E-07 0.00E+00 0.00E+00
Chlorobenzene HAP 2.10E-05 0.00E+00 0.00E+00
Chloroethane(Ethyl HAP 1.10E-05 5.70E-04 0.00E+00 0.00E+00
Chloroform 31 1.00E-07 0.00E+00 0.00E+00
Chloromethane(Methyl 'HAP 1.10E-04 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
' Dibenzofuran NA 3.60E-07 O:00E+00 0.00E+00
Diethylphthalate HAP 1.40E-06 2.40E-04 of 0.00E+00 0.00E+00
Dimethylphthalate HAP 7.80E-07 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 0.00E+00 0.00E+00
Ethylbenzene HAP 2.10E-05 4.40E-05 of 0.00E+00 0.00E+00
Formaldehyde 51 7.50E-02 b 0.00E+00 0.00E+00
Iodomethane(Methyl Iodide) HAP 9.30E-05 ar 0.00E+00 0.00E+00
Isophorone HAP 3.00E-05 ae 0.00E+00 0.00E+00
Lead NA 1.50E-04 ah 0.00E+00 0.00E+00
Wp-Xylene HAP 1.30E-04 6.70E-05 of 0.00E+00 0.00E+00
Manganese 62 2.90E-04 ag 2.90E-04 ah 0.00E+00 0.00E+00
Mercury 66 9.60E-05 ag 7.50E-06 ah 0.00E+00 0.00E+00
Naphthalene HAP 6.90E-06 6.50E-05 0.00E+00 0.00E+00
Nickel 75 7.20E-05 ah 0.00E+00 0.00E+00
o-Xylene HAP 4.70E-05 ac 5.80E-05 0.00E+00 0.00E+00
Perchloroethylene at 0.00E+00_ 0.00E+00
(Tetrachloroethene) 81 2.80E-06
Phenol 82 3.50E-05 ac 8.60E-05 a< 0.00E+00 0.00E+00
Phosphorus HAP 9.80E-04 ag 0.00E+00 0.00E+00
Selenium NA 2.30E-04 ah 0.00E+00 0.00E+00
Styrene 91 1.00E-07 ac 2.00E-05 ac 0.00E+00 0.00E+00
Toluene 97 2.50E-04 ae 1.60E-04 de 0.00E+00 0.00E+00
Total Fluorides 50 6.10E-01 c 0.00E+00 0.00E+00
Trichlorofluoromethane 100 1.40E-05 - 0.00E+00 0.00E+00
Vinyl acetate HAP 1.00E-07 ae 0.00E+00 0.00E+00
a Emission factors from AP-42,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
ab Table 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.
"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.
ab Table 11.3-7 for natural gas-fired kilns.
a`Factor is from AP42 Background Document testing at
Marseilles Brick which has the same type of kiln
Soluble Chromate Compounds is the regulated NC TAP
b Emission factors from AP-42,Section 1.4,7/98. The emissions factor in in lb/mmft 3 of gas. The actual gas rate:
Formaldehyde Emission Factor=
0.0 MMBW/hr/1020 Btu/ft 3*10'Btu/MMBtu/10^(ft 3/MMft3)= 0.0000 mmft3/hr
` Using AP-42 background information,assume that total fluorides emission factor is 60%of the HF emission factor
Also DAQ requires that total fluorides include HF,therefore TF=fluorides+HF(lb/yr)
TF=((0.381 lb/ton*0.60)+0.381 lb/ton)*Brick Production ton/yr*(1 -CE)
d Testing was performed on Kiln 4 on February 10,2006. Emissions Factors are as follows:
Process weight rate during test 19.93 tonthr
Support Calculations File: El 2012-Moncure.xlsx
Printed:6/272013 Page 6 of 35 Sheet Brick-BH(ES-K3K G12)NG&Coal

I
Highest Run
Emissions Rate Emission Factor
Pollutant Tested(lblhr) (lb/ton) -
HF* 7.6 0.381
HCl* 1.16 0.058
PM 2.25 0.113
PM filterable 2.25 0.113
.SO2** 0.56 0.029
' *Total Fluorides are 60%of HF
**SOZ data was from a September 27,2004 engineering test on Kiln 3 with'
a process weight rate of: 19.58 tons/hr
'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
Ap-42 Emission Factor:Section 1.1 Table 1.1-3 38S lb/ton coal fired
Sulfur Content of Fuel 1.000 %
S02 EF= 38 lb/ton coal fired
I d J
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:
Average
Emissions Rate Emission Facto
i Pollutant Tested,(Ib/hr) (Ib/ton)
PM 6.1 0.412
-- PM, 3 0.203
PMZs 3 0.203
Support Calculations File: El2012-Moncure.xlsx
Printed:6/27/2013 Page 7 of 35 Sheet Brick-BH(ES-K3K G12)NG&Coal

Title: 2012 Air Emission Inventory
Source ID#: ES-K3D1,ES-K3D2,ES-K3D3
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
Source: ES-K3D1,ES-K3D2,ES-K3D3 Brick Dryers 1,2,and 3 on Kiln 3
2011 Actual Production: - Tons/yr
Brick Dryer Fuel: NG/Propane
2011 Annual
Emission Factora 2011 Emission Emission
Pollutant (lb/ton fired bricks produced) Rate(lb/yr) Rate(TPY)
PM 0.187 lad 0.00 0.00
PM-10 0.187 lad
0.00 0.00
PM-2.5 0.187 lad 0.00 0.00
SO2 l 0.00
NOx 0.098 laa 0.00 0.00
VOC 0.03 lab 0.00 0.00
CO28'O.3 I lac 0.00 1 0.00
Formaldehyde 1.55E-01 l 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 Factor is from AP-42 Background Document testing at Marseilles Brick
which has the same type of kiln.
ad Table 11.3-1 for brick dryer.
b The formaldehyde emissions from the dryer are included in the kiln calculation.
Support Calculations File: El 2012-Moncure.xlsx
Printed:6/2MO13 Page 8 of 35 Sheet: Brick-Bli(ES-M—G12)(total)

Lb 'O % VOA
b'I s
W d
-4q�p
�o ov
boL'b�d c •41�+►�6� oS
LL9 'S� be,ogI '/L Ql-Wd
q b*'s** 'o V"d
• �� a 'GL �'�SS�B� Z "/ Z'�g5'8E OS'U Ov S-E%/ 77961
L r 'hzb '1 Lam'/GL
is•osg 'ss sS '�SZ '// SS 'O bL'9f '*Z /5w cw
I� •LI� '6L /S'Z�'9'l 1-'p•0 rd' �LS ZP/ z� s-9,-/1 b.>_
68'�St 'lL bz•���'� �/� 'o °�'o2s 'c.% f� 'I o� W�
b� '9db 'Ob 6Z''05
�S/ ' S21Y 74otp,
to 0000b r

Tide: 2012 Air Emission Inventory
Source ID#: ES-K4K
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1"0009
Brick Processing System-Brick Haven-Kiln 4
Source: ES-K4K Kiln 4
Actual Brick Production: 80,382 Tons/yr
Coal Fired 3,253 Tons/yr
Brick Kiln Fuel: Coal/NG
60%Coal
40%Natural Gas
Control Eff.of HF 90% (NESHAP Requirement)
Uncontrolled Uncontrolled
Emission Emission
I
TAP NO. Factor for Ref Factor for Tested Total
Coal from AP- Natural Gas Emission Annual Annual
Pollutant 42 from AP42 Ref Factors Ref Emissions Emissions
(lb/ton) (lb/ton) (lb/ton) (lb/yr) (ton/yr)
PM 4.12E-01 B 80528.96 4.03E+01
PM-10 2.03E-01 g 63705.83 3.19E+01
PM-2.5 2.03E-01 g 63705.83 3.19E+01
SO2 38.000 f 2.86E-02 d 124533.59 6.23E+01
NOx 8.13E-01 65373.75 3.27E+01
VOC 2.40E-02 ad 2.40E-02 ad 1929.17 9.65E-01
CO 8.00E-01 ab 0.83 ai 65270.18 3.26E+01
Chlorine 29 1.30E-03 of 104.50 5.22E-02
HF 59 3.81E-01 d 3065.24 1.53E+00
HCl 57 5.82E-02 d 4678.531 2.34E+00
I I 1-Trichloroethane 68 1.70E-05 az 4.70E-06 of 9.71E-01 4.86E-04
(methylchloroform)
Methylene Chloride 69 8.00E-07 u 6.43E-02 3.22E-05
Perchloroethylene 81 2.80E-06 of 2.25E-01 1.13E-04
(Tetrachloroethene)
1,1-dichloroethane HAP 5.00E-06 m 4.02E-01 2.01E-04
1,4-dichlorobenzene 36 3.20E-06 u 4.80E-05 of 1.70E+00 8.49E-04
2-butanone(MEK) 70 2.50E-04 m 2.20E-04 of 1.91E+01 9.57E-03
2-Hexanone NA 9.40E-07 m 8.50E-05 of 2.78E+00 1.39E-03
2-methylphenol(cresol) 35 2.20E-06 m 1.77E-01 8.84E-05
2-methylnaphthalene NA 1.70E-06 - 5.70E-05 of 1.91E+00 9.57E-04
Antimony NA 2.70E-05 ah 2.17E+00 1.09E-03
Acetone NA 6.80E-04 - 1.70E-03 of 8.75E+01 4.37E-02
Arsenic 9 1.30E-04 ag 3.10E-05 ah 7.27E+00 3.63E-03
Benzene 12 2.90E-04 m 2.90E-03 az 1.07E+02 5.36E-02
Benzoic Acid 2.50E-04 - 2.01E+01 1.00E-02
Beryllium 16 1.60E-05 as 4.20E-07 ah 7.85E-01 3.93E-04
Bis(2-ethylhexyl)phthalate; az 2.00E-03 of 6.78E+01 3.39E-02
di(2-ethylhexyl)phthalate 39 7.30E-OS
Bromomethane(Methyl HAP 2.40E-05 a` 1.93E+00 9.65E-04
Bromide)
Butylbenzylphthalate NA 1.20E-06 a` 1.80E-05 of 6.37E-01 I 3.18E-04
Support Calculations File: El 2012-Moncure.xlsx
Printed:6/27/2013 Page 9 of 35 Sheet: Brick$H(ES-K4K_G12)NG&Goal

Cadmium 23 1.50E-05 ah 1.21E+00 6.03E-04
Carbon Disulfide 27 2.30E-06 4.30E-05 of 1.49E+00 7.47E-04
Carbon tetrachloride 28 1.00E-07 - 8.04E-03 4.02E-06
Chlorobenzene HAP 2.10E-05 - 1.69E+00 8.44E-04
Chloroethane(Ethyl HAP 1.10E-05 u 5.70E-04 of 1.89E+01 9.43E-03
Chloride)
Chloroform 31 1.00E-07 " 8.04E-03 4.02E-06
Chloromethane(Methyl HAP 1.10E-04 az 6.70E-04 of 2.68E+01 1.34E-02
Chloride)
Soluble Chromate 5.10E-05 ah 4.10E+00 2.05E-03
Compounds
Cobalt 2.10E-06 ah 1.69E-01 8.44E-05
Dibenzof Iran NA 3.60E-07 2.89E-02 1.45E-05
Diethylphthalate HAP 1.40E-06 - 2.40E-04 If 7.78E+00 3.89E-03
Dimethylphthalate HAP 7.80E-07 - 6.27E-02 3.13E-05
Di-n-butylphthalate HAP 1.40E-04 of 1.13E+01 5.63E-03
Di-n-octylphthalate 1.20E-05 - 9.65E-01 4.82E-04
Ethylbenzene HAP 2.10E-05 u 4.40E-05 of 2.43E+00 1.21E-03
Formaldehyde 51 # 7.50E-02 b g7$ �,�0E-93� 9.52E-07
Iodomethane(Methyl HAP 9.30E-05 of 7.48E+00 3.74E-03
Iodide)
Isophorone HAP 3.00E-05 - 2.41E+00 1.21E-03
Lead NA 1.50E-04 ah 1.21E+01 6.03E-03
M-/p-Xylene HAP 1.30E-04 u 6.70E-05 of 8.42E+00 4.21E-03
Manganese 62 2.90E-04 ag 2.90E-04 ah 2.33E+01 1.17E-02
Mercury 66 9.60E-05 ag 7.50E-06 ah 4.87E+00 2.44E-03
Naphthalene HAP 6.90E-06 M 6.50E-05 - 2.42E+00 1.21E-03
Nickel 75 7.20E-05 ah 5.79E+00 2.89E-03
o-Xylene HAP 4.70E-05 - 5.80E-05 4.13E+00 2.07E-03
Perchloroethylene of 2.25E-01 1.13E-04
(Tetrachloroethene) 81 2.80E-06
Phenol 82 3.50E-05 " 8.60E-05 4.45E+00 2.23E-03
Phosphorus HAP 9.80E-04 ag 7.88E+01 3.94E-02
Selenium NA 2.30E-04 ah 1.85E+01 9.24E-03
Styrene 91 1.00E-07 - 2.00E-05 - 6.48E-01 3.24E-04
Toluene 97 2.50E-04 - 1.60E-04 u 1.72E+01 8.60E-03
Total Fluorides 50 6.10E-01 c 4.90E+03 2.45E+00
Trichlorofluoromethane 100 1.40E-05 u 1.13E+00 5.63E-04
Vinyl acetate HAP 1.00E-07 az 8.04E-03 4.02E-06
'Emission factors from AP-42,Section 11.3,8/97
"Table 11.3-1 for uncontrolled coal-fired and natural gas-fired kilns.
PM for condensible,PM= 0.59 lb/ton ? �Z Oaf
f`OG . \
Table 11.3-3 for coal-fired and natural gas-fired kilns.
rfQ�d� C ` l �G Ralf
"Table 11.3-4 for coal-fired and natural gas-fired kilns
ad Table 11.3-5 for brick kilns. r
"Table 11.3-6 for coal-fired ki Ins.
®.C7'76kq/r 7�702 M/✓t 5�J
arTable 11.3-6 for natural gas-fired kilns
ae Table 11.3-7 for coal-fired kilns. ? (�
'h 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
'3 Soluble Chromate Compounds is the regulated NC TAP
b Emission factors from AP-42,Section 1.4,7/98. The emissions factor in in lb/mmft 3 of gas. The actual gas rate:
Formaldehyde Emission Factor=
25.9 MMBtu/hr/1020 Btu/ft 3 k 104 Btu/MMBtu/10^(ft 0.0254 mmft3/hr
Support Calculations File: El 2012-Moncure.xlsx
Printed:6127/2013 Page 10 of 35 Sheet: Brick-BH(ES-K4K_G12)NG&Coal

`Using AP-42 background information,assume that total fluorides emission factor is 60%of the HF emission factor
Also DAQ requires that total fluorides include HF,therefore TF=fluorides+HF(lb/yr). The estimate also includes the Control Efficiency
TF=((0.381 lb/ton*0:60)+0.381 lb/tan)*Brick Production ton/yr*(I-CE)
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
J Highest Run
Emissions Rate Emission Factor
Pollutant Tested(lb/hr) (lb/ton)
HF* 7.6 0.381
HCl* 1.16 0.058
PM 2.25 0.113
PM filterable 2.25 0.113
- S02** 0.56 0.029
*Total Fluorides are 60%of HF
**SOZ data was from a September 27,2004 engineering test on Kiln 3 with
a process weight rate of 19.58 tons/hr
`Test Results of Tested Highest run from Kiln and Dryer from Nov.11,2004 Indiana stack test=
4
NOx Emission Factor= 9.67 lb/hr / 11.89 ton/hr
i
NOx Emission Factor= 0.813 lb/ton
r AP-42 coal combustion
Ap-42 Emission Factor:Section 1.1 Table 1.1-3 38S lb/ton coal fired
i
Sulfur Content of Fuel 1.000 %
— S02 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
4
Emission Factors are as follows:
Average
- Emissions Rate Emission Factor
Pollutant Tested(Ib/hr) (lb/ton)
PM 6.1 0.412
PMia 3 _0.203
PMu 3 0.203
I
I
i
Support Calculations File: El 2012-Monwre.xlsx
Printed:6/27/2013 Page 11 of 35 Sheet Brick-BH(ES-K4K G12)NG&Coal

Title: 2012 Air Emission Inventory
Source ID#: ES-K4D1,ES-K4D2,ES-K4D3
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
Source: ES-K4D1,ES-K4D2,ES-K4D3 Brick Dryers 1,2,and 3 on Kiln 4
2011 Actual Production: 80,382 Tons/yr
Brick Dryer Fuel: NG/Propane
2011 Annual
Emission Factor'(lb/ton fired 2011 Emission Emission
Pollutant bricks produced) Rate(Ib/yr) Rate(TPY)
PM 0.187 lad 15031.43 7.52
PM-10 0.187 ad 15031.43 7.52
PM-2.5 0.187 ad 15031.43 7.52
SO2
NOx 0.098 as 7877.44 3.94
VOC 0.03 lab 2411.46 1.21
CO -0, acO,3 2, 6 Ll-2S
Formaldehyde 1.55E-01 b 24,q IS 4-2
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 Factor is from AP-42 Background Document testing at Marseilles Brick
which has the same type of kiln.
ad Table 11.3-1 for brick dryer.
b The formaldehyde emissions from the dryer are included in the kiln calculation.
Support Calculations File: El 2012-Moncure.xlsx
Printed:612712013 Page 12 of 35 Sheet: Brick-BH(ES-K4K_G12)(total)

-- o�T�T v 4 xz;;^_;3 xx x n� m op o nnnQ IS
n m mmm a N <zy�gq +� my
gg9g �qg. q ;�"' n�i a �
� n
3
W 5.
F oR4
NN�io°°eSmZ b tenon'°
p
y yNy y p y p O y>�
ySb q
> A SQgQ'm
W .q. O W Oq.$S W SAS S A u V 0 .V. mA NaN
bbb +ppm+bop+m ypm o o mCm me cmm mb ypm m ypm ypmm�ipm�m ypmm tnm+pm pm+m+pm m+pm }pm m m mm m Sn+pm m Jm.�TOM �C, m m}pmm apmm♦pm $�_ R,�
m
0000000000 00000eo 0000000000000000000000 00 000000 � 0000000
N
pccc ceco 'J�e�1
W 8888889�^41
0000000 0000000 0000000000000000000000000 000000�tz �7m.
assssssssss sssssss sssssssssasasgsssssssssss ssssssss�� ��
mtmmmmmtmmmmm mmmmmmmm mmmmmmmmmtmmmmmmmmmmmmmmmm mmmmmmmtm
y W �
^A^q—JO A N OAUN Aq�p NOo^JOA W O—ONr
Q'pC. pO..!!w y A ttJJ '-b N Eo>J i.+N.N.m m •i.A+�J w�—. pC. pp
OmAb A 8 $J P
mmmmmmmmmmm mmmmmmm mmmmmmmmmmmmmmmmmmmm m m mmm mt�mt7. mcy+ mm.�+� mmmmmmmaA
�tp 25
O:++r lJ pAyy$ypp.y,.pN++ ypUy per++p
ee �O m �00000 A
Pp—Orm wrm Ce 8 AP g..J A App V F H P:-O$r-m 5.t rl r•� :!C poeO p A N V oo^IJ J "V
m mmmmmmmmm mmmmmmm mmmm mmm m mm mm m mmm m Ammmm m m mmmmmmm`mm
1. 0,
J.- ao "'�" $ 8 NNu> en8°°R$o8o>N OaOp00� m m mmm mmmm�nc�m tnmm8 >
tammm m�mmm mmm
mm mmmmmmm mmmmmmmmmmmm�mmmmmmm
�w���o����b �����ob ������������s�b��s�� s � ��� ba��oba�� �����mi�m i �
Atn�+^w V AON^ 0�.1 W..NNA A AO NNOwO...y W w �p�nw oo
y� O �n ppmm J A W yy W NNw byy N ((...�ANN N A ATJ_
�� O Q.b b ^S A SAD W A S�W$ SM A ANi�A N-A W N y
mmmmmmmmmt7r m mmmmmmm mm mmmmmmm mmmmmmm�nm m m mmm mmm$mAmm,lm., °� N o,^A °$ @
J$ms wsssbw� bbews sw�bws�W�w��uNRSSws oJ,OVJ,1:
y Oo V

Title: 2012 Air Emission Inventory
Source ID#: ES-Coal-CC
1 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: 3,253 tpy
Uncontrolled Annual
Emission
Emission Factor Rate(lb/ r) Emission
Pollutant. p y
b/ton) Rate(TPY
PM 1.10 3.58E+01 1.79E-02
PM-10 1.10 3.58E+01 1.79E-02
PM-2.5 1.10 3.58E+01 1.79E-02
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: El 2012-Moncure.xlsx
Printed:6/27/2013 Page 14 of 35 Sheet: ES-Coal Crusher

Title: 2012 Air Emission Inventory
Source ID#: ES-WFS
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
Wood Fuel/Sawdust System
Source: ES-WFS Wood Fuel/Sawdust System
Hours of Operation 160 hrs
Wood Fuel/Sawdust System
- - Control: CD-SD-DC1 Dust Collector
Description: Two conveyors,which feed materials to the two screens,are both controlled by a dust collector.
EPN: EP-SD-DC1
Source: ES-SD-SCI W 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
Bagfilter Efficiency= 99%'
Emissions Before Control
PM Emissions=Emissions After Control/(1-Efficiency)
PM Emissions= 18.0 lb/hr
Emissions After Control
PM Emissions=Exit Concentration* 1 lb/7,000 gr*Flow Rate*60 min/hr
PM Endssions= 0.180 lb/hr
I
28.8 lb/ r
-I
Support Calculations File: El 2012-Moncure.xlsx
Printed:6/27/2013 Page 15 of 35 Sheet: Controlled New WFS(G-21)

Wood Fuel/Sawdust System
Controls: CD-SD-DC2- Dust Collector(2300 cfm)
Description: Dust collector is used for the PM exhaust from the hammermill and cyclone.
EPN: EP-SD-DC2
Source: ES-SD-CYC Cyclone
ES-SD-HM Hammermill
Variables: Hours of Operation
Factors:
Exit Concentration= 0.01 gr/dscf
Flow Rate for System= 2345 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
PM Emissions= 0.201 lb/hr
32.16 lb/yr
Support Calculations File: El 2012-Moncure.xlsx
Printed:6/27/2013 Page 16 of 35 Sheet: Controlled New WFS(G-21)

Wood Fuel/Sawdust System
Controls: CD-SD-BVI Bin Vent Filter
Description: Storage silo,which is connected to a bin vent filter,is used as storage for the product.
EPN: EP-SD-BVl
Source: ES-SD-SDS Sawdust Silo
Variables: Hours of Operation
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 lb/hr
Emissions After Control
PM Emissions=Exit Concentration* 1 lb/7,000 gr*Flow Rate*60 min/hr
IPM Emissions= 0.034 lb/hr
5.5 lb/yr
Support Calculations File: El 2012-Moncure.xisx
Printed:6/27/2013 Page 17 of 35 Sheet: Controlled New WFS(G-21)

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
Source: ES-SD-SH Surge Hopper
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
Emissions After Control
PM Emissions=Exit Concentration* 1 lb/7,000 gr*Flow Rate*60 min/hr
PM Emissions= 0.034 lb/hr
5.5 lb/yr
Total WFS Emissions
rotal
Pollutant (Controlled) TPY
PM 7.19E+01 3.60E-02
PM-10 7.19E+01 3.60E-02
PM-2.5 7.19E+01 3.60E-02
Support Calculations File: El 2012-Moncure.xlsx
Printed:612 712 01 3 Page 18 of 35 Sheet: Controlled New WFS(G-21)

Title: 2012 Air Emission Inventory
Source ID#: Clay Handling
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
Source: ES-CH Clay Handling Equi�ment
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 P vat t6r
Actual Raw Material Processed 106,067 tpy
Maximum Hours of Operation 1,440 hrs/yr� �
Control Efficiency for PM 0 % No Control Devices
ID Description
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#4(clay handling
equipment 200 tph)NSPS
F-FCS Finishing Conveyor#5(clay handling
equipment 200 tph)NSPS
Pollutant Actual Emissions
Name (lbs/ r) (tous/ r)
PM 2,652 1.33
PM-10 244 0.12
PM-2.5 244 0.12
Support Calculations File: El 2012-Moncure.xlsx
Printed:6/27/2013 Page 19 of 35 Sheet: Clay Handling(G-71)

Title: 2012 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)
0.0251b/ton* 106067 tpy = 2651.68 lbs/yr
PM Actual Emissions(tons/yr)
2651.675 lbs/yr/20001b/ton = 1.33 tpy
PM-10 Actual Emissions(lbs/hr)
0.0023 lb/ton*106067 tpy = 243.954 lbs/yr
PM-10 Actual Emissions(tons/yr)
243.9541 lbs/yr/2000lb/ton = 0.12 tpy
PM-2.5 Actual Emissions(lbs/hr)
0.0023 lb/ton*106067 tpy = 243.954 lbs/yr
PM-2.5 Actual Emissions(tons/yr)
243.9541 lbs/yr/2000lb/ton = 0.12 tpy
Support Calculations File: El 2012-Moncure.xlsx
Printed:6/27/2013 Page 20 of 35 Sheet: Clay Handling(G-71)

4
2012 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)^l.4](1-control eff/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 AP42
PM<=30 microns:
0.74*0.0032*[(15 mph/5)^1.3/(10/2)AIA]= 1.04E-03 lb/ton
PM<=10 microns:
0.35*0.0032*[(15 mph/5)^1.3/(10/2)AIA]= 4.91E-04 lb/ton
PM<=2.5 microns:
0.053*0.0032*[(15 mph/5)^1.3/(10/2)^1.4]= 7.43E-05 lb/ton
Basis: All emission sources for the proposed grinding room are listed below.
i
Control Efficiency for PM 0 % No Control Devices
The following source will be subject to NSPS.
Emissions estimated using the Drop Equations from AP42
Location Descri hon Throughput Drops
Pi
From Cape Fear to ES-C Conveyor 97,234
Brickhaven 1
i
Pollutant Potential Emissions(per emission source)
Name (Ibsyyr) (fons/yr)
PM 100.90 0.05
PM-10 47.72 0.02
PM-2.5 7.23 0.00
Emissions based on Drop Equations Equations @ 200 tph,which is the process weight rate for 13rickhaven's
existing Grinding Room.
Support Calculations File: El 2012-Moncure.xlsx
Printed:6/2 712 01 3 Page 21 of 35 Sheet: intersiteConv(Clay Handling)

SAMPLE CALCULATIONS
Grinding&Screening Emissions
PM Potential Emissions(lbs/yr)
0.001 lb/ton*97234 tpy* 1 drop= 100.90 lbs/hr
PM Potential Emissions(tons/yr)
101 /2000lb/ton = 0.05 tons/yr
TOTAL EMISSION CALCULATIONS FOR CLAY HANDLING
Pollutant Potential Emissions(per emission source)
-- Name (lbs/yr) (tons/yr)
PM 2752.58 1.38
PM10 291.68 0.15
PM2.5 251.18 0.13
f
Support Calculations File: El 2012-Moncurexlsx
Printed:6/27/2013 Page 22 of 35 Sheet: IntersiteConv(Clay Handling)

Title: 2012 Air Emission Inventory
Source ID#: ES-CR-5,ES-CR-6,and ES-CR-7
Description: Texturing Operations
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
Texturing Operations
Sand Blasting Cabinets
Parameter Value
Actual Brick Production-CIF 6,937 tons/yr
Actual Brick Production-BH 80,382 tons/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 6937 tpy
Actual Brick Production.Rate-Brickhaven 80382 tpy
Scale Up Factor Potentials 1
Two Texturing Operations
- Controlled by CD-CR6BF,CD-CR7BF,CD-CR7BF2 and CD-CR7BF3.
EMISSION CALCULATIONS
LL Brick Haven Brick Haven Cape Fear Total
Pollutant Actual'Emissions Actual Emissions . Actual Emissions
Name (lbs/ r) (tons% r). (lbs[ r) (tons/ r) (lbs/ r) (tons/ r)
PM 289.38 0.145 24.97 0.012 314.35 0.157
PM-10 289.38 0.145 24.97 0.012 314.35 0.157
PM-2.5 1 289.38 0.145 1 24.97 0.012 314.35 0.157
-1 Support Calculations File: El2012-Moncurexlsx
Printed:6/27/2013 Page 23 of 35 Sheet: Text(G-69)

Title: 2012 Air Emission Inventory
Source ID#: ES-CD-8
Description: Rotary Coatings Dryer
Facility: General Shale Brick,k,Inc.
Location: Moncure,NC
Facility ID#: 1900009
Source: ES-CD-8 Rotary Coatings Dryer
Description: Sand is dried in the rotary coatings dryer
EPN: EP-CD-8
Controls: CD-CDBBF
Variables: Hours.of Operation
Dryer Fuel: Natural Gas with Propane/Air Standby
Dryer Gas Rate(MMBtu/hr)= 0.25 MMBtu/hr
Hours of Operation= 400 hrs
Bagfilter Control Efficiency= 99.9%
Heating Value for Natural Gas= 1020 Btu/ft3
2011 Gas Usage(Calculated 9.80E-02 mm ft3/yr
based upon hours of operation)_
Uncontrolled Emission Factor Emissions Emissions
Pollutant nb/mmft3) Ref Rate(lb/yr) Rate(tpy)
PM 7.6 3 6.04E+01 3.02E-02
PM-10 7.6 3 6.04E+01 3.02E-02
PM-2.5 7.6 3 6.04E+01 3.02E-02
SO2 6.00E-01 1 5.88E-02 2.94E-05
NOx 100 1 9.80E+00 4.90E-03
VOCs 5.5 1 5.39E-01 2.70E-04
CO 84 1 8.24E+00 4.12E-03
2-Methylnaphthalene 2.40E-05 1 2.35E-06 1.18E-09-
3-Methylchloranthrene 1.80E-06 1 1.76E-07 8.82E-11
7,12-Dimethylbenz(a)anathracene 1.60E-05 1 1.57E-06 7.84E-10
_ Acenaphthene 1.80E-06 1 1.76E-07 8.82E-11
Acenaphtylene 1.80E-06 1 1.76E-07 8.82E-11
Anthracene 2.40E-06 1 2.35E-07 1.18E-10
Benz(a)anthracene 1.80E-06 1 1.76E-07 8.82E-11
Benzene 2.10E-03 1 2.06E-04 1.03E-07
Benzo(a)pyrene 1.20E-06 1 1.18E-07 5.88E-11
Benzo(b)fluoranthene 1.80E-06 1 1.76E-07 8.82E-11
Support Calculations File: El 2012-Moneurexlsx
Printed:6/2 7120 1 3 Page 24 of 35 Sheet Dryer(ES-CD-6)

f
Benzo(g,h,I)perylene 1.20E-06 1 1.18E-07 5.88E-11
Benzo(k)fluoranthene 1.80E-06 1 1.76E-07 8.82E-II
Butane 2.1 1 2.06E-01 1.03E-04
Chrysene 1.80E-06 1 1.76E-07 8.82E-11
Dibenzo(a,h)anthracene 1.20E-06 1.18E-07 5.88E-11
Dichlorobenzene 1.20E-03 1 1.18E-04 5.88E-08
Ethane 3.1 1 3.04E-01 1.52E-04
Fluoranthene 3.00E-06 1 2.94E-07 1.47E-10
Fluorene 2.80E-06 1 2.75E-07 1.37E-10
Formaldehyde 7.50E-02 1 7.35E-03 3.68E-06
Hexane 1.8 1 1.76E-01 8.82E-05
Indeno(1,2,3-cd)pyrene 1.80E-06 1 1.76E-07 8.82E-11
Naphthalene 6.10E-04 1 5.98E-05 2.99E-08
Pentane 2.6 1 2.55E-01 1.27E-04
Phenanathrene 1.70E-05 1 1.67E-06 8.33E-10
Propane 1.6 1 1.57E-01 7.84E-05
Pyrene 5.00E-06 t- 4.90E-07 2.45E-10
Toluene 3.40E-03 1 3.33E-04 1.67E-07
Arsenic 0.00E+00 2 0.00E+00 0.00E+00
Barium 4.40E-03 1 4.31E-04 2.16E-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 t 8.24E-06 4.12E-09
Copper 8.50E-04 1 8.33E-05 4.17E-08
CO2 1.20E+05 2 1.18E+04 5.88E+00
Lead 5.00E-04 1 4.90E-05 2.45E-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 1 2.25E-01 1.13E-04
Molybdenum 1.10E-03 1 1.08E-04 5.39E-08
N2O 2.20E+00 1 2.16E-01 1.08E-04
Nickel 0.00E+00 , 2 0.00E+00 0.00E+00
Selenium 2.40E-05 1 2.35E-06 1.18E-09
Vanadium 2.30E-03 1 2.25E-04 1.13E-07
Zinc 2.90E-02 1 2.84E-03 1.42E-06
r 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(AP-42,Section
1.4)and factors for industrial sand dryers(AP-42,Section 11.19)
i Support Calculations File: El 2012-Monoure.xlsx
Printed:6/27/2013 Page 25 of 35 Sheet: Dryer(ES-CD-8)

" i
Parameter Value
Maximum Hourly Coatings Rate 3.45 ton/hr
Maximum Annual Coatings Rate 30,222.00 ton/yr
Industrial Sand Dryer Emission
Factor* 2.00 lb/ton
PM/PM-10/PM-2.5 Emissions= 3.45 ton/hr*21b/ton
- PM/PM-10/PM-2.5 Emissions= 6.90 lb/hr
Y -
PM/PM-10/PM-2.5 Emissions= 30222 ton/yr*21b/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 AP-42,Section 11.19 was selected for use. It is felt that
this is a conservative factor because the factor is for mined quartzite that is
processed into sand,which is normally a dirtier operation than is conducted for
coatings at brick plants.
_.I
Support Calculations File: El 2012-Moncure xlsx
Printed:6/27/2013 Page 26 of 35 Sheet Dryer(ES-CD-8)

Title: 2012 Air Emission Inventory
Source ID#:ES-VS1,-VS2,-VS3,-VS4,&-VS5
Facility: General Shale Brick,Inc.
Location: Moncure,NC
i
Facility ID Al 19.00009
Vacuum Systems
The vacuum systems,which all connect to a bag filter,are used to collect particulate matter from the empty kiln cars
at both the Brickhaven and Cape Fear Plants. VS-3 is used to remove sand at the sand seal discharge at the
Brickhaven Plant.
FACTORS Exit Concentration= 0.01 gr/dscf
Flow Rate for System= 1400 cfm
Bagfilter Efficiency= 99.9%
G-70 Hours of Operation-Cape Fear= 160 hr/yr
- - (IES-VS1)
Hours of Operation-Brick Haven= 270 hr/yr
` ('IES-VS2)
Total 430 hr/yr
G-22 Hours of Operation-Brick Haven= 1,920 hr/yr
(IES-VS3)-Kiln 3 Hi-Vac
Hours of Operation-Brick Haven= - hr/yr
(IES-VS4&-VS5)
Total 1,920 hr/yr "
Emissions Before Control
PM Emissions=Emissions After Control/(1 -Efficiency)
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 lb/hr
f PM-2.5 Emissions= 0.120 lb/hr
F
- ENIISSION CALCULATIONS
Actual Emissions=PM Emissions,lb/hr(After Control)*Hours of Operation,hr/yr
G-70(IES-VS 1&-VS2)
Pollutant Actual Emissions-BII Actual Emissions-CF Total Actual Emissions
Name bs/ tons/ (lbs/yr) (tons/yr) (Ibs/yr) (tons/yr)
PM 32.40 0.016 19.20 0.010 51.60 0.026
PM-10 32.40 0.016 19.20 0.010 51.60 0.026
PM-2.5 32.40 0.016 19.20 0.010 51.60 0.026
G-22(IES-VS3,-VS4&-VS5)
Pollutant Actual Emissions=VS3 . .Actual.Emissions-VS4&.-VS5 Total Actual Emissions
Name bs/ tons/ (Ibs/yr) (tons/yr). (Ibs/ 'yr) (tons/yr)
_ PM 230.40 0.115 0.00 0.000 230.40 0.115
PM-10 230.40 0.115 0.00 0.000 230.40, 0.115
PM-2.5 230.40 0.115 0.00 0.000 230.40 0.115
Support Calculations File: E12012-Moncure.xlsx
Printed:6/27/2013 Page 27 of 35 Sheet: Vacuums(G-22&G-70)

Title: 2012 Air Emission Inventory
Source ID#c Storage Tanks
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
I
Tank Tank Breathing Working 'Total
height diam Capacity Throughput Losses Losses Emissions
Aescription/Contents Size (ft) (ft) (gal) (gpy) Turnovers . (lb/yr) (lb/yr) pb/yr)
Diesel 1,000 7 5 881 20,000 22.69 0.14 0.53 0.67
Gasoline 1,000 7 5 1,028 1,200 1.17 310.55 11.50 322.05
Waste Oil 275 5.25 3 225 200 0.89 15.60 0.61 16.21
- Motor Oil 160 4.5 2.5 129 250 1.95 21.07 1.67 22.74
Brick Oil 350 6.5 3 291 2,500 8.60 15.60 23.17 38.77
- Gear Oil 350 6.55 3 346 150 0.43 15.60 0.61 16.21
29,300 Total(lb/yr)= 416.65
Total(ton/yr)= 0.208
Support Calculations Fle: El2012-Moncurexlsx
Printed:6/27/2013 Page 28 of 35 Sheet: Storage Tanks(G-144)

Title: 2012 Air Emission Inventory
Source ID H: ESBP-FAS
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ED N:1900009
Controlled Controlled Controlled _
Source PM „PMta PM23
Emission
Classification Control Emission Emission Emission
Source Code(SCC) DevrcelD Factor Factor Factor Throughput PM Emissions PMtoEmissions PMuEmissions
Description (lb/ton) pb/ton) (lb/ton) ( y) (lb/y) (spy) (b/y) (spy) (lbly) (tpy)
Ff ash Si 3-05-011-06 bin vent 0.0089 0.0049 0.0049 0 0.00E+00 1 0.00E+00 0.00E+00 I 0.00E+00 0.00E+00 0.00E+00
a Controlled PM emission factors for aggregate transfer,pneumatic flyssh loading,pneumatic loading of cement silo,weigh hopper loading,and mixer loading fiom AP42,Section 11.12-
Conaete Batch Operations,(10/01). -
Flyasb
SBoFi ' Flyasb Silo Emissions
Ha2ardoas Emission
Air Factor Example Calculations:
Pollutant Ob/tan) (Ibty)' (toy)
Arsenic 1.00E-06 0.00E+00 0.00E+00 PM Potential Emissions 0bs(yr)
Berylliu 9.04E-08 0.00E+00 0.00E+00 0.009lb/ton+Otpy=lbs/yr 0lbs/yr
Cadmium 1.98E-08 0.00E+00 0.00E+00
Chromi 1.22E-06 0.00E+00 0.00E+00 PM Potential Emisdoas(tons/yr)
Lead 5.20E-07 0.00E+00 0.00E+00 . 0lbs/yr+(1 ton2000 lb)= 0.00E+00 tons/yr
Mangan 2.56E-07 0.00E+00 0.00E+00
Nickel 2.28E-06 0.00E+00 0.00E+00
Phospho 3.54E-06 0.00E+00 0.00E+00
Selenium 7.24E-08 0.00E+00 0.00E+00
i
Support Calculations FHe:El 2012-Moncoe.ift
Printed:6272013 Page 29 of 35 Shoot:Flyash Silo

Title: 2012 Air Emission Inventory
Source ID N: ES-BP-CS
Facility: General Shale Brick,Inc. ,
Location: Moncure,NC
Facility ID ft:1900009
Controlled Controlled
Source PM PMte Controlled
Classificatio Control Emission Emission PMssEmissi
Emission n Code Device ID -
Source (SCC) Factor' Factor^ an Factad Throughput PM Emissions PM,.Emissions PM,3 Emissions
Description (lb/ton) (lb/ton) Bb/ton) (tpy) (lb/y) (tpy) (1b/) (.y) (Ib/y) F (tpy)
Cement Si3-05-011-07 bin vent 0.00099 0.00034 0.00034 0 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00
a Controlled PM emission factors for aggregate tamfa,pneumatic flyash loading,pneumatic loading of wnent silo,weigh hopper loading,and mixer loading from AP-42,Section
11.12-Concrete Batch Operations,(10101). -
Cement Silo
Hazardous Emission Cement Silo Emissions!"
Air Factors Example Calculations:
Pollutant (lb/ton) (ib/y) 'Opy) -
Arsenic 4.24E-09 0.00E+00 0.00E+00 PM Potential Emissions(Ibsfyr)
Berylliu 4.86E-10 0.00E+00 0.00E+00 0.000991b/ton•Otpy=Ibsfyr 0 Ibs/yr
Cadmium 4.86E-10 0.00E+00 0.00E+00
Chromilm 2.90E-07 0.00E+00 0.00E+00 PM Potential Emissions(tonsfyr)
Lead 1.09E-08 0.00E+00 0.00E+00 0 Ibs/yr (I ton/20001b)_ 0.00E+00 tons/yr
Mangan 1.17E-07 0.00E+00 0.00E+00 - -
ISckel 4.18E-05 0.00E+00 0.00E+00
Phospho - - -
Selenium - -
i
1 ,
1
l
printed:6f272013 Support Calculations File.,E12012-Moncure.xim
Page 30 of 35 Street:Cenrent Silo

Title: 2012 Air Emission Inventory
Source ID N: ES-BP-BM -
Facility: General Shale Brick,Ins -
- Location: Moncure,NC -
Facility ID N: 1900009
_ Controlled Controlled Controlled
Source. PM PMro PMss
Classification Control Device ID- Emission Emission Emission .
Emission Sour Code(SCC) Factor Factor Factory Itroughput PM Emissions P111ro Emissions PMrs Emissions
Description (lb/ton) Ob/ton) (lb/ton) (tpy) pb/y)' (tpy) - (lb/y) I (tpy) pb/y) (tpy)
Mixer Loading 3-05-011-09 ba filter 0.011 0.0038 0.0038 0 0.00E+00 0.00E+00 0.00E+00 I 0.00E+00 0.00E+00 0.00E+00
a Controlled PM emission factors for aggregate transfer,pnamatic flyash loading,pneu-tic loading of ccrnent sib,weigh topper load n&and mixer loading from AP42,Section 11.12-
Concrcle Batch Operations,(10(01).
Batch Mxee Emission Batch MxerEmissiont -
Hazardous Air Factors Example Calculations:
Pollutant (lb/ton) (Ib/y) _ (tpy)
Arsenic 1.87E-08 0.0000 0.00E+00 PM Potential Emisslom(lbslyr)
Beryllium - _ - - 0.0111Wton•0tpy=Ibs(yr 0 ftlyr
Cadmium 7.10E-10 0.0000 0.00E+00
Chromium 1.27E-07 0.0000 0.00E+00 PM Potential Emisslons(tomlyr)
Lead 3.66E-08 0.0000 0.00E+00 0Ibslyr•(1 ton(2000 lb)_ 0.00E+00 tonstyr
Manganese 3.78E-06 0.0000 0.00E+00
Mckel 2A8E-07 0.0000 0.00E+00
Phosphorus 1.20E-06 0.0000 0.00E+00
Selenium - -
t
I I
Printed:6272013 Support Celcolations File:El 20124M-cura.:dsx
Page 31 of 35 Sheet Balch Mixer

I -
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
Hours of Operation: 0 hrs
Factors:
Exit Concentration= 0.01"gr/dscf
Flow Rate for System= 5000 cfin
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/hr
PM/PM-10/PM-2.5 Emissions= 0.429 lb/hr
0.00 lb/yr'
0.00 tpY
Pollutant Controlled Actual Emissions. .
Name (lbs/hr) (lbs/yr) (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
i
Support Calculations File: El 2012-Moncure.xlsx
Printed:6/27/2013 Page 32 of 35 Sheet: Rumbler

i
Title: 2012 Air Emis
Source ID M Summary
Facility: General Shale
Location: Moncure,NC
Emissions Summary
Storage Total Total
Pollutant Cas Numbelixer Rumbler Tanks (lb/yr) MY)
- PM 0 0.00E+00 1.04E+05 51.88
PM-10 00 0.00E+00 8.45E+04 42.24
PM 2.5 00 0.00E+00 8.44E+04 42.22
j' S02 1.26E+05 62.91
NOx 7.58E+04 37.91
VOC 2.08E-01 6.01E+03 3.00
CO J 9.02E+04 1 45.09
1,4-dichlorobenzene 106-46-7 1.70E+00 8.49E-04
2-butanone(MEK) 78-93-3 2.07E+01 1.03E-02
-" 2-methylphenol(cresol) 95-48-7 1.77E-01 8.84E-05
Acrylonitrile 107-13-1 1.32E-01 6.59E-05
Antimony kNTIMONYCi 2.19E+00 1.09E-03
Arsenic ARSENICCP]00 7.41E+00 3.71E-03
Benzene 71-43-2 1.11E+02 5.56E-02
Benzo(a)pyrene 30-32-8 1.18E-07 5.88E-11
Beryllium BERYLCPD 7.87E-01 3.94E-04
1 Bis(2-ethylhexyl)phthalate;di(2-
117-87-7 6.88E+01 3.44E-02
eth lhex 1)phthalate
Bromomethane(Methyl Bromide) 74-83-9 .2.23E+00 1.12E-03
Cadmium CADMIUMCP00 1.36E+00 6.79E-04
1 Carbon Disulfide 75-15-0 1.62E+00 8.09E-04
Carbon tetrachloride 56-23-5 1.07E-02 5.34E-06
Chlorine 7782-50-5 1.04E+02 0.05
J Chloroethane(Ethyl Choroethane) 75-00-3 , 1.89E+01 9.43E-03
Chloroform 67-66-3 ( 1.07E-02 5.34E-06
Chloromethane(Methly Chloride) 74-87-3 3.66E+01 1.83E-02
Chromium CROMCPD00 4.43E+00 2.22E-03
-- Cobalt 7440-48-4 1 1.69E-01 8.44E-05
Diethylphthalate 84-66-2 7.78E+00 3.89E-03
Dimethylphthalate 131-11-3. 1 6.27E-02 3.14E-05
Di-n butylphthalate 84-74-2 1.14E+01 5.68E-03
File: El2012-Moncure.xlsx
Printed:6/27/2013 Sheet: Summary

Storage Total Total
Pollutant Cas Number xer Rumbler Tanks (lb/yr) (TPY)
Ethylbenzene 100-41-4 2.50E+00 1.25E-03
Fluorine 7782-41-4 1 0.00E+00 0.00E+00
Formaldehyde 50-00-0 1.80E+01 8.99E-03
Hexane 110-54-3 1.76E-01 8.82E-05
Hydrazine 302-01-2 0.00E+00 0.00E+00
HF 7664-39-3 4.66E+03 2.33E+00
HCI 7647-01-0 5.86E+03 2.93E+00
Hydrogen Sulfide 7783-06-4 0.00E+00 0.00E+00
Iodomethane(Methyl Iodide) 74-88-4 9.14E+00 4.57E-03
Lead LEADCPDSD0 1.29E+01 6.44E-03
M-/p-Xylene 108-38-3/1064 8.63E+00 4.31E-03
Manganese MANGCPD410 2.66E+01 1.33E-02
111-Trichloroethane(methylchloroform) 71-55-6 9.75E-01 4.87E-04
Methylene Chloride 75-09-2 I 4.94E-01 2.47E-04
Mercury MERCCPDS 4.95E+00 2.47E-03
Naphthalene 91-20-3 2.42E+00 1.21E-03
Nickel NICKCPDSDO 6.02E+00 3.01E-03
o-Xylene 95-47-6 4.18E+00 2.09E-03
Ozone 0.00E+00 0.00E+00
Perchloroethylene(Tetrachloroethene) 127-18-4 2.28E-01 1.14E-04
Phenol 108-95-2 5.15E+00 2.57E-03
Phosphine 7803-51-2 0.00E+00 0.00E+00
Phosphorus 7723-14-0 �00 8.26E+01 4.13E-02
Selenium SEC 1.88E+01 9.41E-03
Styrene 100-42-5 6.77E-01 3.39E-04
Toluene 108-88-3 2.02E-1-01 1.01E-02
Total Fluorides(including BF) 16984-48-8 6.78E+03 3.39E+00
Trichlorofluoromethane 75-69-4 1.13E+00 5.66E-04
Vinyl acetate 108-05-4 9.36E-03 4.68E-06
;
Xylene 1330-20-7 1.28E+01 6.40E-03
-- File: El 2012-Moncure.xlsx
Printed:6127/2013 Sheet: Summary

Fugitive Emission Sources
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
.6/27/2013,FUG-EI-Monc.doc Page 36 of 36

APPENDIX A
TANKS 4.09 CALCULATIONS
i
General Shale Brick, Inc. -Moncure, NC Facility I CY 2012 Emissions Inventory
Trinity Consultants

TANKS 4.0:9d
Emissions Report - Detail Format
Tank Indentification and Physical Characteristics
Identification
User Identification: Waste Oil-Moncure
City: Moncure
State: North Carolina
Company: General Shale Brick, Inc.
Type of Tank: Vertical Fixed Roof Tank
Description: 275 Gallon Waste Oil Tank
Tank Dimensions
Shell Height(ft): 5.25
Diameter(ft): 3.00
Liquid Height(ft): 4.25
Avg, Liquid Height(ft): 4.25
Volume(gallons): 224.73
Turnovers: 0.89
Net Throughput(gal/yr): 200.00
Is Tank Heated(y/n): N
Paint Characteristics
-Shell Color/Shade: Gray/Medium
Shell Condition Good
Roof Color/Shade: Gray/Medium
Roof Condition: Good
Roof Characteristics
Type: Dome
Height(ft) 0.50
Radius(ft)(Dome Roof) 3.00
Breather Vent Settings
Vacuum Settings(psig): -0.03
Pressure Settings(psig) 0.03
Meterological Data used in Emissions Calculations:Raleigh,North Carolina(Avg Atmospheric Pressure=14.53 psia)

i
i
TANKS 4.0.9d
Emissions Report - Detail FormaF
Liquid Contents of Storage Tank i
Waste Oil -Moncure-Vertical Fixed Roof Tank
Moncure, North Carolina
Liquid
Daily Llquid Surf. Bulk Vapor Liquid Vapor
Temperature(deg F) Temp Vapor Pressure(psia) Mol. Mass Mass Mol. Basis for Vapor Pressure
Mixture/Component Month Avg. Min. Max. (deg F) Avg. Min. Max. Weight. Fract, Fract. Weight Calculations
Crude oil(RVP 5) All 68.49 57.95 79.03 62.36 3.3910 2.7639 4.1272 50.0000 207.00 Option 4:RVP=5
i
i
i
it
i
I
1
I
I'
l
I
I
1

TANKS 4.0.9d
Emissions Report - Detail Formal:
Detail Calculations (AP-42)
Waste Oil Moncure -Vertical Fixed Roof Tank j
Moncure, North Carolina
Annual Emission Calcaulations
j'
Standing Lasses(Ib): 15:6006 ! '
Vapor Space Volume(cu ft): 8.9012
Vapor Density(lb/cu ft): 0.0299
Vapor Space Expansion Factor. 0.1968 I:
Vented Vapor Saturation Factor: 0.8155
i
Tank Vapor Space Volume: �
Vapor Space Volume(cu ft): 8.9012
Tank Diameter(ft): 3.0000
Vapor Space Outage(it): 1.2593
Tank Shell Height(ft): 5.2500
Average Liquid Height(ft): 4.2500
Roof Outage(ft): 0.2593
Roof Outage(Dome Roof)
Roof Outage(ft): 0.2593
Dome Radius(ft): 3,0000
Shell Radius(ft): 1.5000 _
Vapor Density
Vapor Density(lb/cu ft): 0.0299
Vapor Molecular Weight(lb/lb-mole): 50.0000
Vapor Pressure at Daily Average Liquid L
Surface Temperature(psia): 3.3910 _
Daily Avg.Liquid Surface Temp.(deg.R): 528.1618
Daily Average Ambient Temp.(deg.F): 59.2833
Ideal Gas Constant R
(psia cuft/(lb-mol-deg R)): 10.731
Liquid Bulk Temperature(deg.R): 522.0333
Tank Paint Solar Absorptance(Shell): 0.6800
Tank Paint Solar Absorplance(Roof): 0.6800
Daily Total Solar Insulation
Factor(Btu/sqft day): 1,393.0797
Vapor Space Expansion Factor
Vapor Space Expansion Factor. 0.1968 �f l
Daily Vapor Temperature Range(deg.R): 42.1602
Daily Vapor Pressure Range(psia): 1.3633
Breather Vent Press.Setting Range(psia): 0.0600
Vapor Pressure at Daily Average Liquid
Surface Temperature(psia): 3.3910
Vapor Pressure at Daily Minimum Liquid
Surface Temperature(psia): 2.7639
Vapor Pressure at Daily Maximum Liquid
Surface Temperature(psia): 4.1272
Daily Avg.Liquid Surface Temp.(deg R): 526.1618
Daily Min.Liquid Surface Temp.(deg R): 517.6217
Daily Max.Liquid Surface Temp.(deg R): 538.7018
Daily Ambient Temp.Range(deg.R): 21.7167 'I
Vented Vapor Saturation Factor
Vented Vapor Saturation Factor: 0.8155 III'i
Vapor Pressure at Daily Average Liquid:
Surface Temperature(psia): 3.3910
Vapor Space Outage(ft): 1.2593

Working Losses(lb): 0.6055
Vapor Molecular Weight(lb/lb-mole): 50.0000
Vapor Pressure at Daily Average Liquid
Surface Temperature(psia): 3.3910 ;!`
Annual Net Throughput(gallyr.): 200.0000
Annual Turnovers; 0.6900
Turnover Factor: 1.0000
Maximum Liquid Volume(gal): 224.7266
Maximum Liquid Height(ft): 4.2500
Tank Diameter(fl): 3.0000
Working Loss Product Factor: 0.7500
I;
Total Losses(lb); 16.2061
I.
ji
I '
I
III
I
ddVddV� ,
f�
1
1
t
u

--- - - - - - -- --- - - -- -- '' - - - -- — - i t — - - - - -- - - --- - -
IyyH
Pi�
TANKS 4.0.9d
Emissions Report - Detail For.mat:!
Individual Tank Emission Totals
Emissions Report for: Annual
ul;
a;
Waste Oil - Moncure-Vertical Fixed Roof Tank 5;
Moncure, North Carolina �II
Losses(lbs) l l
Components Working LO-S—Sli Breathing Loss Tota�
Crude oil(RVP 5) 0.61 15.60 16.21
'II?
li
,lii •
o !
IlI1 .
• I�I I
NL!
Ala
i�
I
i
� II
1
I
I j
I
!'t
�!f
li 1
ri

TANKS 4.0.9dII
Emissions Report - Detail Forma;
Tank Indentification and Physical Chara( eriistics
Identification
User Identification: 2010 Moncure-Motor Oily{
City: Moncure ii l
State: North Carolina
Company: General Shale Brick, Inc.
Type of Tank: Vertical Fixed Roof Tank ;ii I'
Description: 2010 Emission Inventory Moncure Plant 160 gallon Motor Oil AST
Tank Dimensions
Shell Height(ft): 4.50
Diameter(ft): 2.50
Liquid Height(ft): 3.50
Avg.Liquid Height(ft): 3.50 it
Volume(gallons): 128.52
Turnovers: 1.95 '
Net Throughput(gal/yr): 250.00
Is Tank Heated(y/n): N
L,I .
Paint Characteristics
Shell Color/Shade: Gray/Medium
Shell Condition Good 1
Roof Color/Shade: Gray/Medium l
Roof Condition: Good I!
it
Roof Characteristics
Type: Dome a
Height(ft) 0.50
Radius(ft)(Dome Roof) 2.50 !i
�I�I
Breather Vent Settings
Vacuum Settings"(psig): -0.03
Pressure Settings(psig) 0.03
Meterological Data used in Emissions Calculations:Raleigh,North Carolina(Avg Atmospheric Pressure=14.53 psia) !I?
I! ,
.;I a
ikl
I;6I.
ii�l q

,•I I
TANKS 4.0.9d
Emissions Report- Detail Forma,�ii
Liquid Contents of Storage Tanll
2010 Moncure - Motor Oil -Vertical Fixed Roof Tank ; V
Moncure, North Carolina !'
LiquidI i!
Daily Liquid Surf. Bulk Vapor LiquidlI Vapor
Temperature(deg F) Temp Vapor Pressure(psia) Mol. Mass +i Mass Mol. Basis for Vapor Pressure
Mixture/Component Month Avg. Min. Max. (deg F) Avg. Min. Max. Weight. Fract. +�I Fract. Weight Calculations
'�is
Gasoline(RVP 7) All 68.49 57.95 79.03 62.36 .4.1311 3.3417 5.0648 68.0000 1 p 92.00 Option 4:RVP=7,AST Slope=3
,l
i

TANKS 4.0.9d ' '
i.
Emissions Report . Detail Formal
Detail Calculations (AP-42)
2010 Moncure -Motor Oil -Vertical Fixed Roof Tank
Moncure, North Carolina }
Annual Emission Calcaulalions
Standing Losses(lb): 21.0715
Vapor Space Volume(cu ft): 6.2014 it
Vapor Density(lb/cu ft): 0.0496
Vapor Space Expansion Factor: 0.2398
Vented Vapor Saturation Factor: 0.7833 t
Tank Vapor Space Volume:
Vapor Space Volume(cu ft): 6.2014
.Tank Diameter(ft): '2.5000 _• t 1
Vapor Space Outage(ft): 1.2633 li I
Tank Shell Height(ft): 4.5000
Average Liquid Height(ft): 3.5000 ;;+
Roof Outage(ft): 0.2633 t
Roof Outage(Dome Roof) {,
Roof Outage(ft): 0.2633 i
Dome Radius(ft): 2.5000 G
Shell Radius(ft): 1.2500
i
Vapor Density
Vapor Density(lb/cu f): 0.0496 ti i
Vapor Molecular Weight(lb/lb-mole): 68.0000
Vapor Pressure at Daily Average Liquid
Surface Temperature(psia): 4.1311
Daily Avg.Liquid Surface Temp.(deg.R): 528.1618
Daily Average Ambient Temp.(deg.F): 59.2833 l
Ideal Gas Constant R
(psia tuft/(lb-mot-deg R)): 10.731 �'(
Liquid Bulk Temperature(deg.R): 522:0333
Tank Paint Solar Absorptance(Shell): 0.6800
Tank Paint Solar Absorptance(Roof): 0.6800
Daily Total Solar Insulation
Factor(Btu/sgft day): 1,393.0797 !'
Vapor Space Expansion Factor )I
Vapor Space Expansion Factor: 0.2398 l'
Daily Vapor Temperature Range(deg.R): 42.1602
Daily Vapor Pressure Range(psia):_ 1.7231 i
Breather Vent Press.Setting Range(psia): 0.0600
Vapor Pressure at Daily Average Liquid
Surface Temperature(psia): 4.1311
Vapor Pressure at Daily Minimum Liquid
Surface Temperature(psia):; 3.3417 l
Vapor Pressure at Daily Maximum Liquid
Surface Temperature(psia): 5.0648
Daily Avg.Liquid Surface Temp.(deg R): 528.1618
Daily Min,Liquid Surface Temp.(deg R): 517.6217
Daily Max.Liquid Surface Temp.(deg R): 538.7018
Daily Ambient Temp.Range(deg.R): 21.7167 i�{
Vented Vapor Saturation Factor {I
Vented Vapor Saturation Factor: 0.7833
Vapor Pressure at Daily Average Liquid:
Surface Temperature(psia): 4.1311
Vapor Space Outage(ft): 1.2633

i
Working Losses(lb): 1.6721 i
Vapor Molecular Weight(lb/lb-mole): 68.0000
Vapor Pressure at Daily Average Liquid ;
Surface Temperature(psia): 4.1311
Annual Net Throughput(gallyr.): 250.0000
Annual Turnovers: 1.9452
Turnover Factor: 1.0000 ti
Maximum Liquid Volume(gal): 128.5201 i
Maximum Liquid Height(ft): 3.5000
Tank Diameter(ft): 2.5000 (,
Working Loss Product Factor: 1.0000 tI
ICI.
Total Losses(lb): 22.7436
�I
tl
s,
ii
i
1
:fII
�t
fir!r
�I
1i)
'.I
i�
;i
i
1
I`I
.i�
i�
l

Y
TANKS 4.0.9d
Emissions Report - Detail Forma''
Individual Tank Emission Totals,;,;
Emissions Report for: Annual11.
2010 Moncure - Motor Oil -Vertical Fixed Roof Tank
Moncure, North Carolina
Losses(lbs)
Components Working Loss Breathing Loss Total'E "issions
Gasoline(RVP 7) 1.671F 21.0711
I;
�f
i
i
'�j

TANKS 4.0.9d
Emissions Report-Brief Format
Individual Summaries
Emissions Report for:Annual
General Shale Moncure Gear Oil-Vertical Fixed Roof Tank
Losses(lbs)
Components WbrkingKo:ss:s]j Breathing Lossil Total Emissions
Crude oil(RVP 5) 0.45 15.60 16.05
i

r
I,
�i
TANKS 4.0.9d �°!
Emissions*Report - Detail Formal
Tank Indentification and Physical Chara9 eristics
Identification
User Identification: Moncure-Gasoline
City: Moncure
State: North Carolina
Company: General Shale Brick,Inc.
Type of Tank: Vertical Fixed Roof Tank
Description: 1,000 gallon Gasoline AST ;
i
Tank Dimensions
Shell Height(ft): 7.00
Diameter(ft): 5.00
Liquid Height(ft): 7.00
Avg. Liquid Height(ft): 3.50
Volume(gallons): 1,028.16
Turnovers: 1.17 r
Net Throughput(gal/yr): 1,200.00
Is Tank Heated(y/n): N I
Paint Characteristics r
Shell Color/Shade: Gray/Medium
Shell Condition Good I
Roof Color/Shade: Gray/Medium
Roof Condition: Good
S
Roof Characteristics
Type: Dome ;
Height(ft) 0.50
Radius(ft)(Dome Roof) 5.00 a'
1�
Breather Vent Settings
Vacuum Settings(psig): 70.03
Pressure Settings(psig) 0.03 i!
a,
Meterological Data used in Emissions Calculations:Raleigh,North Carolina(Avg Atmospheric Pressure=14.53 psia)
p,
�i
n I
�I
I

�i
TANKS 4.0.9d
Emissions Report - Detail Format,
Liquid Contents l!
q of Storage Tank „
Moncure -Gasoline-Vertical Fixed Roof Tank
Moncure, North Carolina
Liquid
Daily Liquid Surf. Bulk Vapor Liquid , Vapor
Temperature(deg F) Temp Vapor Pressure(psia) Mol. Mass i; Mass Mol. Basis for Vapor Pressure
Mixture/Component Month Avg. Min. Max. (deg F) Avg. Min. Max. Weight. Fract. Fract. Weight Calculations
Gasoline(RVP 10) All 68.49 57.95 79.03 62.36 6.0979 4.9830 7.4035 66.0000 92.00 Option 4:RVP-10,ASTM Slope=3
�i
I
i
f�f
�I
.SLt
i�6 f
R
��L t
'l 1
I�I

I
TANKS 4.0.9d
Emissions Report - Detail Format
Detail Calculations (AP-42)
Moncure-Gasoline-Vertical Fixed Roof Tank
Moncure, North Carolina l
n,
Annual Emission Calcaulations
Standing Losses(lb): 310.5547
Vapor Space Volume(cu ft): 73.6965
Vapor Density(lb/cu ft): 0.0710
Vapor Space Expansion Factor. 0.3598 +'
Vented Vapor Saturation Factor: 0.4519 it
Tank Vapor Space Volume:
m
Vapor Space Volume(cu ft): 73.6965
Tank Diameter(ft): 5.0000 n
Vapor Space Outage(ft): 3.7533
Tank Shell Height(ft): 7.0000
Average Liquid Height(ft): 3.5000 tr
Roof Outage(ft): 0.2533
t
Roof Outage(Dome Roof) ;a� •
Roof Outage(ft): 0.2533
Dome Radius(ft): 5.0000
Shell Radius(ft): 2.5000
3
Vapor Density
Vapor Density(lb/cu ft): 0.0710
Vapor Molecular Weight(lb/lb-mole): 66.0000
Vapor Pressure at Daily Average Liquid
Surface Temperature(psia): 6.0979
Daily Avg.Liquid Surface Temp.(deg.R): 528.1618 y
Daily Average Ambient Temp.(deg.F): %2833
Ideal Gas Constant R a
(psia cuff/(lb-mol-deg R)): 10.731
Liquid Bulk Temperature(deg.R): 522.0333 i?
Tank Paint Solar Absorptance(Shell): 0.6800 k
Tank Paint Solar Absorptance(Roof): 0.6800
Daily Total Solar Insulation
Factor(Btu/sgft day): 1.393.0797
�i
Vapor Space Expansion Factor ti
Vapor Space Expansion Factor: 0.3598
Daily Vapor Temperature Range(deg.R): 42.1602
Daily Vapor Pressure Range(psia): 2.4206
Breather Vent Press.Setting Range(psia): 0.0600
Vapor Pressure at Daily Average Liquid r
Surface Temperature(psia): 6.0979
Vapor Pressure at Daily Minimum Liquid
Surface Temperature(psia): 4.9830
Vapor Pressure at Daily Maximum Liquid
Surface Temperature(psia): 7.4035
Daily Avg.Liquid Surface Temp.(deg R): 528.1618 :2
Daily Min.Liquid Surface Temp.(deg R): 517.6217
Daily Max.Liquid Surface Temp.(deg R): 538.7018
Daily Ambient Temp.Range(deg.R): 21.7167
Vented Vapor Saturation Factor
Vented Vapor Saturation Factor: 0.4519
Vapor Pressure at Daily Average Liquid:
Surface Temperature(psia): 6.0979
Vapor Space Outage(ft): 3.7533

Working Losses(lb): 11.4989
Vapor Molecular Weight(lb/lb-mole): 66.0000
Vapor Pressure at Daily Average Liquid
Surface Temperature(psia): 6.0979
Annual Net Throughput(gaVyr.): 1,200.0000
Annual Turnovers: 1.1671
Turnover Factor: 1.0000
Maximum Liquid Volume(gal): 1,028.1610
Maximum Liquid Height(ft): 7.0000
Tank Diameter(ft): 5.0000
Working Loss Product Factor: 1.0000
Total Losses(lb): 322.0536
dl
}
J+
f
T
j�
f
i,
r'
w
`i
f;
T

TANKS 4.0.9d
Emissions Report - Detail Formal
Individual Tank Emission Totals`'
Emissions Report for: Annual
Moncure -Gasoline-Vertical Fixed Roof Tank
Moncure, North Carolina
Losses(lbs)
Components Working Loss Breathing Loss Total Emissions
Gasoline(RVP 10) =1 11.5011 310.55 ; 322.05
i'
4�
4
j.
i.

I
TANKS 4.0.9d
Emissions Report - Wail Forma
Tank Indentification and Physical Characteristics
Identification
User Identification: Moncure-Diesel
City: Moncure
State: North Carolina
Company: General Shale Brick, Inc.
Type of Tank: Vertical Fixed Roof Tank
Description: 1,000 gallon Diesel AST
Tank Dimensions ;•
Shell Height(ft): 7.00
Diameter(ft): 5.00
Liquid Height(ft): 6.00
Avg.Liquid Height(ft): 6.00
Volume(gallons): 881.28
Turnovers: 22.69
Net Throughput(gal/yr): 20,000.00
Is Tank Heated(y/n): N
Paint Characteristics
Shell Color/Shade: Gray/Medium
Shell Condition Good
Roof Color/Shade: Gray/Medium
Roof Condition: Good
Roof Characteristics
Type: Dome
Height(ft) 0.50
Radius(ft)(Dome Roof) 5.00
Breather Vent Settings
Vacuum Settings(psig): -0.03
Pressure Settings(psig) 0.03
Meterological Data used in Emissions Calculations:Raleigh,North Carolina(Avg Atmospheric Pressure=14.53 psia)

TANKS 4.0.9d
Emissions Report - Detail Format
Liquid Contents of Storage Tank;
Moncure - Diesel -Vertical Fixed Roof-Tank
Moncure, North Carolina
Liquid
Daily Liquid Surf. Bulk Vapor Liquid Vapor
Temperature(deg F) Temp Vapor Pressure(psia) Mol. Mass Mass Mol. Basis for Vapor Pressure
Mixture/Component Month Avg. Min. Max. (deg F) Avg. Min. Max. Weight. Fract. Fract. Weight Calculations
Distillate fuel oil no.2 All 68.49 57.95 79.03 62.36 0.0086 0.0061 0.0117 130.0000 188.00 Option 1:VP60=.0065 VP70=.009
i

TANKS 4.0.9d
Emissions Report - Detail Format•
Detail Calculations (AP-42)
Moncure - Diesel -Vertical Fixed Roof Tank
Moncure, North Carolina
Annual Emission Calcaulations
Standing Losses(lb): 0.1351
Vapor Space Volume(cu ft): 24.6091
Vapor Density(lb/cu ft): 0.0002
Vapor Space Expansion Factor: 0.0761
Vented Vapor Saturation Factor: 0.9994
Tank Vapor Space Volume:
Vapor Space Volume(cu ft): 24.6091
Tank Diameter(ft): 5.0000
Vapor Space Outage(ft): 1.2533
Tank Shell Height(ft): 7.0000
Average Liquid Height(ft): 6.0000
Roof Outage(ft): 0.2533
Roof Outage(Dome Roof)
Roof Outage(ft): 0.2533
Dome Radius(ft): 5.0000
Shell Radius(ft): 2.5000
Vapor Density
Vapor Density(lb/cu ft): 0,0002
Vapor Molecular Weight(lb/lb-mole): 130.0000
Vapor Pressure at Daily Average Liquid
Surface Temperature(psia): 0.0086
Daily Avg.Liquid Surface Temp.(deg.R): 528.1618
Daily Average Ambient Temp.(deg.F): 59.2833
Ideal Gas Constant R
(psia cult/(lb-mol-deg R)): 10,731
Liquid Bulk Temperature(deg.R): 522.0333
Tank Paint Solar Absorptance(Shell): 0.6800
Tank Paint Solar Absorptance(Roof): 0.6800
Daily Total Solar Insulation
Factor(Btu/sqft day): 1,393.0797
Vapor Space Expansion Factor
Vapor Space Expansion Factor. 0.0781
Daily Vapor Temperature Range(deg.R): 42.1602
Daily Vapor Pressure Range(psia): 0.0056
Breather Vent Press.Setting Range(psia): 0.0600
Vapor Pressure at Daily Average Liquid
Surface Temperature(psia): 0.0086
Vapor Pressure at Daily Minimum Liquid
Surface Temperature(psia): 0.0061
Vapor Pressure at Daily Maximum Liquid
Surface Temperature(psla): 0.0117
Daily Avg.Liquid Surface Temp.(deg R): 528.1618
.Daily Min.Liquid Surface Temp.(deg R): 517.6217
Daily Max.Liquid Surface Temp.(deg R): 538,7018
Daily Ambient Temp.Range(deg.R): 21.7167
Vented Vapor Saturation Factor
Vented Vapor Saturation Factor; 0.9994
Vapor Pressure at Daily Average Liquid:
Surface Temperature(psia): 0.0086
Vapor Space Outage(ft): 1.2533

Working Losses(lb): 0.5338
Vapor Molecular Weight(lb/lb-mole): 130.0000
Vapor Pressure at Daily Average Liquid
Surface Temperature(psia): 0.0086
Annual Net Throughput(gal/yr.): 20,000.0000
Annual Turnovers: 22.6942
Turnover Factor: 1.0000
Maximum Liquid Volume(gal): 881.2809
Maximum Liquid Height(ft): 6.0000
Tank Diameter(ft): 5.0000,
Working Lass Product Factor: 1.0000
Total Losses(lb): 0.6689

i
TANKS 4.0.9d
Emissions Report - Detail Format
Individual Tank Emission Totals
Emissions Report for: Annual
Moncure -Diesel -Vertical Fixed Roof Tank
Moncure, North Carolina
Losses(lbs)
Components Working LossI Breathing Loss Total Emissions
Distillate fuel oil no.2 0.53 0.14 0.67

TANKS 4.O.9d
Emissions Report-Detail Format
Tank Indentification and Physical Characteristics
Identification
User Identification: General Shale Moncure-Brick Oil
City: Moncure
State: North Carolina
Company. General Shale Brick,Inc.
Type of Tank: Vertical Fixed Roof Tank
Description: 350-gallon brick oil AST
Tank Dimensions
Shell Height(ft): 6.50
Diameter(ft): 3.00
Liquid Height(ft): 5.50
Avg.Liquid Height(ft): 5.50
Volume(gallons): 290.82
Turnovers: 8.60
Net Throughput(gal/yr): 2,500.00
Is Tank Heated(y/n): N
Paint Characteristics
Shell Color/Shade: Gray/Medium
Shell Condition Good
Roof Color/Shade: Gray/Medium
Roof Condition: Good
Roof Characteristics
Type: Dome
Height(ft) 0.50
Radius(ft)(Dome Roof) 3.00
Breather Vent Settings
Vacuum Settings(psig): -0.03
Pressure Settings(psig) 0.03
Meterological Data used in Emissions Calculations:Raleigh,North Carolina(Avg Atmospheric Pressure=14:53 psia)

TANKS 4.0.9d
Emissions Report-Detail Format
Liquid Contents of Storage Tank.
General Shale Moncure-Brick Oil-Vertical Fixed Roof Tank
Moncure,North Carolina
uquid
Daily L(qud Surf. Bulk Vapor ()quid Vapor
Temperature(deg F) Temp Vapor Pressure(psia) Mol. Mau Mass Mol. Basle for Vapor Pressure
Mixture/ComPonent _ Month Avg. Min. Max. (deg F) Avg. Min. Max. Weight F—L Fract Weight Caladations
Crude oil(RVP 5) M 68.49 57.95 79.03 62.36 3.3910 2.7639 4.1272 50.0000 207.00 Option 4:RVP=5, T

TANKS 4.0.9d
Emissions Report-Detail Format -
Detail Calculations(AP-42)
General Shale Moncure-Brick Oil-Vertical Fixed Roof Tank
Moncure,North Carolina
Annual Emission Calmulabons
Standing Losses(Ib): 15.6006
Vapor Space Volume(cu it): 8.9012
Vapor Density(lb1:1l): 0.U99
Vapor 5'pace Expansion Factor. 0.1968
Vented Vapor Saturation Factor: 6.81655 '
Tank Vapor Space Volume.
Vapor Space Volume(cu 0): 8,9012
Tank Diameter(it): 3.0000
Vapor Space Outage(it): 1.2593
Tank Shell Height(R): 6,5000
Average Uquid Height(it): 5.5000
Roof Outage(8): 0,2593
Roof Outage(Dome RwQ
Roof Outage(0): 0.2593
Dome Radius(it): 3.0000
Shell Rod=(ry: 1.5000
Vapor Density
Vapor Density(Ib/cu M: 0.0299
Vapor Molecular Weight(IbAb-mole): 50.0000
Vapor Pressure at Daily Average Liquid
Surface Temperature(psiaj 3.3910
Daily Avg,Uquid Sudace Temp.(deg.R): 528.1618
DailyAverege Ambient Temp.(deg F): 59.2833
Ideal Gas Constant R
(psis cult y 0bmepdeg R)): 10.731
Uquid Bulk Temperature(deg.R): 522.0333
Tank Paint Solar Absorptance(Shell): 0.6800
Tank Paint Solar Absorplance(R-q: 0.6800
Daily Total Solar Insulation
Factor(StufseR day): 1.393.0797
Vapor Space Expansion Facto _
- Vapor Space Expansion Factor: 0.1988
Daily Vapor Temperature Range(deg.R): 42.1602
Daily Vapor Pressure Range(psia): 1.3633
Breather Vent Press.Setting Range(psia): 0,0600
Vapor Pressure at DaiyAverage Liquid ,
Surface Temperature(psia): 3.3910
Vapor Pressure at Daily Minimum Liquid
Surface Temperature(psia): 2.7639
Vapor Pressure at Daly Maximum Liquid
Surface Temperature(Palo): 4.1272
Daily Avg Uquid Surface Temp.(deg R): 528.1618
Daily Min.Uquid Surface Temp.(deg R): 517.6217
Daily Max.Uquid Surface Temp.(deg R): 538.7018
Daily Ambient Temp.Range(deg R): 21.7167
Vented Vapor Saturation Factor
Vented Vapor Saturation Factor. 0.8155
Vapor Pressure at Daily Average Uquid
Sudace Temperature(psla): 3.3910 _
Vapor Space Outage(it): 1.2593
Working L.-(Iby 7.5691 `
Vapor Molecular Weight(IhAb-mole): 50.0000
Vapor Pressure at Daily Average Liquid
Surface Temperature(peia): 3.39f0
-- Annual Net Throughput(galtyrj: 2.500.0000
Annual Turnovers:: 8.5963
Turnover Factor. 1.0000
Maximum Uquid Volume(gal): 290.8227 _
Maximum Liquid Height(it): 5.5000
Tank Diameter(8): 3.0000
Working Loss Product Factor. 0.7500 -
Total Losses(lb): 23.1698
1
1
I I
i

TANKS 4.0.9d
Emissions Report-Detail Format
Individual Tank Emission Totals
Emissions Report for:Annual
General Shale Moncure-Brick Oil-Vertical Fixed Roof Tank
Moncure,North Carolina
f
Losses(lbs)
Components Working Loss Breathing Loss Total Emissions
Crude oil(RVP 5) 1.5jj 23.17
i