AQ_F_1900009_20140630_EI_Cmb-EI-File

2013 Emissions Inventory Review / Data Tracking Form
Facility Name: General Shale Brick, Inc. - Moncure Facility Facility ID: 1900009
Facility Assigned to: Data Entry: Chatham County
Classification: Stanley Williams DN Confidential Copy Submitted?
Title V 0 ES
NO
Initial Review/Data Entry
® Enter date received into ED. Date Received: fo•/9• ?co 14
® Assigned to appropriate individual. Date Assigned: 6- 30a, 2p/4 Date Due: /per/5a 2G%9�
❑ Paper copy submitted: One copy received with supporting documentation,certification form signed by responsible official,and
appears generally complete;OR
® Electronic copy submitted: All supporting documentation and certification form(with time/date stamp)signed by responsible
official has been received.
Comments:
Inventory Review
❑ All forms and supporting documentation appear to be complete if paper submission(check ED OS data if electronic).
❑ Contact,address,phone number changes entered into I-Beam/Facilities if necessary.
Z All known operating scenarios,control devices,and emission release points have been entered for each emission source(permitted,
insignificant,and unpermitted)or note that the emission source was not operated or not required to report.
® Evaluate"U"sources for significance and address according to policy. .
• Calculations/forms appear to add up correctly.
0 All compliance issues are being addressed(e.g.Toxics limits,above TV thresholds,large emissions increase/decrease,installation
without a permit).
0 All volatile HAPs/TAPs were included in the VOC total.
0 Calculations and control efficiencies appear correct. Emission factors are the best available and most current factors appropriate
for the reporting facility(e.g. stack testing,AP42,etc.).
0 Review facility comments and address any issues.
❑ Update ED(Data Entry Main)if additional information is required(corrections due date and date received).
0 Check all ED QA/QC reports.
0 Comparison with previous emission inventory must be made and outliers(> 10%)must be investigated and explained.
® Put inventory review comments and summarize any changes in ED-Data Entry Main"DAQ internal comments".
0 Print and attach the facility total report.
Date Review Complete: 9.4 a wl4 Signature: 14,LdQ c
Date Submitted to EI Coordinator: 9•//-Zo/4
Date Approved: Q t{( / I 4 Initials:

Facility Total CY 2013 Emission Summary Recorded in ED Facility ID#: 1900009
Facility Name: General Shale Brick,Inc.-Mon cure Faeility Permit#(s): 04384T37
Green House Gases Pollutants (GHG) Actual Emissions %
Tons/Yr
Pollutant CAS
Demini- Change'
mus
Not Not N/A
Reported Reported
CO2 equivalent(sum of individual GHG pollutant emission No GHGs
times their 1995 IPCC Global Warming Potential(GWP), Reported
converted to metric tons)
Criteria Pollutants Actual Emissions
(Tons/Year)
Pollutant CAS CY 2013 CY 2012 Demini- %
from ED from Fees mus Change
CO Co 61.09 56.59 0.5 8.0%
NOx NOx 26.16 23.15 0.5 13.0%
PM(TSP) TSP 64.87 59.38 0.5 9.3%
PMIO PM10 52.08 44.73 0:5 .16.4%
PM2.5 PM2.5 0.487000 0.530000 0.5 -8.1%
S02 Sot 47.52 42.03 0.5 .13..1%
VOC VOC 2.92 3.03 0.5
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPs) (Pounds/Year)
Pollutant CAS CY 2013 CY 2012 Demini- %
from ED from Fees mus Change
ntimony & Compounds(total mass, inc elemental SB) 2.60 2.19 10.0 118.7%
Antimony Unlisted Compounds-Speck Compound SBC-other 2.60 2.19 10.0 18.6%
(Component of SBC)
Arsenic& Compounds(total mass of elemental AS, arsine and 8.70 7.42 0.01 17.3
all inorganic compounds)
Arsenic Unlisted Compounds-Speck Compound ASC-Other 8.70 7.42 0.01 .17.3%
(Component of ASC)
Beryllium & compounds(Total mass) 0.939690 0.788150 1.0 19.2%
Beryllium Metal(unreacted) (Component of BEC) 7440-41-7 0.939690 0.788150 1.0 1.9.2%
Cadmium & compounds(total mass includes elemental metal) 1.44 1.36 0.1 15.9%
09/04/2014 Page 1 of 4

Facility Total CY 2013 Emission Summary Recorded in ED Facility ID #: 1900009
Facility Name: General Shale Brick, Inc. -Moncure Facility Permit#(s): 04384T37
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPs) (Pounds/Year)
Pollutant CAS CY 2013 -CY 2012 Demini-
from ED from Fees mus Change
Cadmium Metal, elemental, unreacted(Component 7440-43-9 1.44 1.36 0.1 6.2%
of CDC)
Chromium-A1UTotal(includes Chromium (VI) categories, 4.91 _ 4.43 0.1 10.8%
metal and others)
Chromic acid(VI) (Component of SolCR6& CRC) 7738-94-5 4.91 4.43 0.01 .1.0.7%
Chromium (VI)Soluble Chromate Compounds (Component of 4.91 . 4.43 0.01 10.8%
CRC)
Chromic acid(VI) (Component of SolCR6& CRC) 7738-94-5 4.91 4.43 0.01 .10.7%
Cobalt& compounds 0.202020 0.168800 1.0 119.7%
Cobalt Unlisted Compounds-Speck Compound COC-Other 0.202020 0.168800 1.0 1.9.7%
(Component of COC)
Lead& compounds 14.43 12.89 1.0 11.9%
Lead Unlisted Compounds-Speck Compound PBC-Other 14.43 12.89 10.0 112.0%
(Component of PBQ
Manganese & compounds 27.90 26.64 10.0 14.7%
Manganese Unlisted Compounds-Speck MNC-other 27.90 26.64 10.0 4.7%
Compound(Component of MNC)
Mercury & Compounds-all total mass includes Hg Vapor 5.83 4.95 0.001 117.8%
Mercury, vapor(Component of HGC) 7439-97-6 5.83 4.95 0.001 1.7.9%
Nickel& Compounds,sum total mass includes elemental 6.93 6.02 1.0 15.1%
Nickel metal(Component ofNIC) 7440-02-0 6.93 6.02 1.0 .15.0%
Polycyclic Organic Matter(Specific Compounds from OAQPS Z90 Z42 1.0 19.8%
or Tip
Naphthalene (Component of 833291POMTV) 91-20-3 2.90 2.42 1.0 19.8%
Acrylonitrile 107-13-1 Not 0.131800 10.0 N/A
Reported
Benzene 71-43-2 128.33 111.08 1.0 .15.5%
Carbon'disulfide 75-15-0 1.79 1.62 10.0 1.0.0%
Carbon tetrachloride 56-23-5 0.009020 0.010680 1.0 -.15.5%
09/04/2014 Page 2 of 4

Facility Total CY 2013 Emission Summary Recorded in'ED Facility ID #: 1900009
Facility Name: General Shale Brick,Inc. -Moncure Facility Permit#(s): 04384T37
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPS) (Pounds/Year)
Pollutant CAS CY 2013 CY 2012 Demini- %
from ED from Fees mus Change
CFC-II (Trichlorofluoromethane) 75-69-4 1.35 1.14 100.0 718.5%
Chlorine 7782-50-5 125.06 104.50 100.0 119.7%
Chloroform 67-66-3 0.009620 0.010680 100.0 1 -9.9%
DEHP(Di(2-ethylhexyl)phthalate) 117-81-7 81.17 68.77 10.0 18.0%
Dibutylphthalate 84-74-2 13.47 11.36 100.0 1 .18.5%'
Dichlorobenzene(p), 1,4- 106-46-7 2.03 1.70 1.0 119.5%
Dimethyl phthalate 131-11-3 0.075040 0.062720 10.0 1,119.6%
Ethyl benzene 100-41-4 2.91 2.50 100.0 1.1.6.2%
Ethyl chloride (chloroethane) 75-00-3 22.57 18.90 -10.0 19.4%
Fluorides (sum of all fluoride compounds as mass of R6984-48-8 5,869.56 7,459.82 10.0 -21.3%
ion)
Formaldehyde 50-00-0 4.71 22.41 10.0 1-79.0%'
Hexane,n- 110-54-3 0.132300 0.176400 100.0 1-25.0%
Hydrogen chloride (hydrochloric acid) 7647-01-0 5,599.26 -5,855.59 100.0 1 -4.4%
Hydrogen fluoride (hydrofluoric acid as mass of HF) 7664-39-3 3,668.48 4,659.31 100.0 -21.3%
(Component of 16984488/Fluorides)
MEK(methyl ethyl ketone, 2-butanone) 78-93-3 22.90 20.63 100.0 11.0%
Methyl bromide (bromomethane) 74-83-9 2.31 2.23 1.0 3.3%
Methyl chloride(chloromethane) 74-87-3 32.13 36.51 1.0 1-12.0%
Methyl chloroform 71-55-6 1.16 0.974610 100.0 19.2%
Methyl iodide (iodomethane) 74-88-4 8.95 9.14 10.0 -2.1%
Methylene chloride 75-09-2 0.076960 0.494390 1.0 -84.4%
Perchloroethylene (tetrachloroethylene) 127-18-4 0.269360 0.227710 100.0 1 18.3%
Phenol 108-95-2 5.33 , 5.14 100.0 3.6%
Phosphorus Metal, Yellow or White 7723-14-0 94.28 82.62 1.0 114.1%
Selenium Compounds SEC 22.13 18.81 10.0 17.6%
Styrene 100-42-5 0.775380 0.677140 100.0 14.5%
09/04/2014 Page 3 of 4

Facility Total CY 2013 Emission Summary Recorded in ED Facility ID #: 1900009
Facility Name: General Shale Brick, Inc. -Moncure Facility Permit#(s): 04384T37
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPS) (Pounds/Year)
Pollutant CAS CY 2013 CY 2012 Demini- %
from ED from Fees mus Change
Toluene 108-88-3 20.59 20.18 100.0 2.0%
Vinyl acetate 108-05-4 0.009620 0.009360 100.0 2.8%
Xylene (mixed isomers) 1330-20-7 10.08 12.85 100.0 -2.1.6%
Xylene, o- 95-47-.6 4.94 4.18 100.0 1.8.3%
Largest Individual HAP Hydrogen chloride(hydrochloric acid) 5,599.26 lbs
Total HAP Emissions 9,929.79 lbs
DAQ's Comments Regarding Inventory
Coal consumption was up 30.99%from the consumption in 2012 and gas consumption was down 31.64%for the same
period. The significant difference in formaldehyde is due to the reduced gas consumption and the fact that the Cape Fear
plant did not operate in 2013,which also accounts for the difference in hydrogen fluoride,fluorides,and methylene
chloride. Facility-wide brick production increased 19.67%for 2013.
09/04/2014 Page 4 of 4

Ai
.......................................................................................................................................................................................................
Igp6D6 q
2013 CALENDAR YEAR EMISSIONS INVENTORY
General Shale Brick, Inc. - Moncure, NC Facility
General Shale Brick
Building The American Dream'
June 2014
Project 143401.0073
NC DENR Raleigh Regional OTlce
Prepared By:
TRINITY CONSULTANTS
One Copley Parkway
Suite 310
Morrisville,NC 27560
[phone]
Tinn. i �- L
comur6fts
Environmental solutions delivered uncommonly well

TABLE OF CONTENTS
SECTION 1: NCDAQ CY 2013 EMISSION INVENTORY AERO FORMS PAGE
CertificationForm.....................................................................................................................................................................................1
Listing of Emission Sources&Control Devices on Permit............................ ....................................:..................................2
EmissionSource&Operating Scenario List....................................................................................................................................9
BrickDryers for Kiln 3 at Brickhaven............................................................................................................................................11
WoodFuel/Sawdust System................................................................................................................................................................13
VacuumSystem-Brickhaven............................................................................................................................................................16
BrickProcessing-Cape Fear.............................................................................................................................................................18
BrickTexturing...........................................................................................................................................:...........................................21
VacuumSystem.......................................................................................................................................................................................23
ClayHandling...........................................................................................................................................................................................25
iDryers for Cape Fear(should be removed)..............:...................................................................................................................27
BrickDryers-Kiln 4.............................................................................................................................................................................29
StorageTanks........................................................................................................:.................................................................................31
BatchMixer...............................................................................................................................................................................................33
CementSilo...............................................................................................................................................................................................35
FlyashSilo.................................................................................................................................................................................................37
- Coatings Dryer.........................................................................................................................................................................................39
CoalCrusher........................................................................................................................................................................................:....41
BrickProcessing-Brickhaven Kiln 3...............................................................................................................................................43
- . Brick Processing-Brickhaven Kiln 3...............................................................................................................................................45
BrickProcessing-Kiln 4....................................................................................................................................................................47
Rumbler....................................................................................................................................:................................................................50
PropaneVaporizer.................................................................................................................................................................................52
FacilityTotals....................................:................:....................................................................................................................................54
iComments.............................................................................:................................................:..................................................................57
SECTION 2: SUPPORTING EMISSION CALCULATIONS
CriticalParameters..................................................:.................................................................................................................................1
BrickProcessing-Cape Fear..........................................................................................
Brick Processing at Brickhaven Kiln 3 (Firing Coal and-NG).....:......................................... ........ ..................3
BrickDryers at Brickhaven Kiln 3......................................................................................................................................................8
Brick Processing at Brickhaven Kiln 4(Natural Gas/Coal).......................................................................................................9
BrickDryers at Brickhaven-Kiln 4................................................................................................................................................12
Brick Summary.................................. ............................................................................................................................14
. .........................
Coal Crusher
General Shale Brick,-Inc. -Moncure, NC Facility I CY 2013 Emissions Inventory
Trinity Consultants
a

Wood Fuel Sawdust System New 16
ClayHandling Equipment....................................................................................................................................................................20
IntersiteConveyer..................................................................................................................................................................................22
BrickTexturing.......................................................................................................................................................................................24
CoatingsDryer.........................................................................................................................................................................................25
VacuumSystem.......................................................................................................................................................................................28
StorageTanks..........................................................................................................................................................................................29
FlyashSilo.....................................................................................................................................................
CementSilo..........:....................................................................................................................................................................................31
BatchMixer...............................................................................................................................................................................................32
Rumbler.....................................................................................................................................................................................................33
Summaryof Emissions.........................................................................................................................................................................34
-Fugitive Sources......................................................................................................................................................................................36
APPENDIX A: TANKS 4.09 CALCULATIONS
General Shale Brick, Inc. -Moncure, NC Facility CY 2013 Emissions Inventory
Trinity Consultants

1
SECTION 1
NCDAQ CY 2013 EMISSION INVENTORY (AFRO) FORMS
General Shale Brick, Inca-Moncure, NC Facility CY 2013 Emissions Inventory
Trinity Consultants
j

COPY of RECORD Date Submitted: 6/19/2014 16:46:44
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 2013
These forms must be comRleted and returned even if the facility did not oRerate or emissions were zero
The legally defined "Responsible Official" of record for your facility is Kevin Ham
This person or one that meets the definition below must sign this certification form.
The official submitting the information must certify that he/she complies with the requirements as specified in Title 15A
NCAC 2Q.0520(b)which references and follows the federal definition.40 CFR Part 70.2 defines a responsible as meaning one
of the following:
1. For a corporation: a president,secretary,treasurer, or vice—president of the corporation in charge of a principal
business function,or any other person who performs similar policy or decision making functions for the overall
operation of one or more manufacturing,production,or operating facilities applying for a or subject to a permit and
either
i.the facilities employ more than 250 persons or have gross annual sales or expenditures exceeding$25
million(in second quarter 1980 dollars); or
ii. the delegation of authority to such representatives is approved in advance by the permitting authority;
2. For partnership or sole propietorship;a general partner or the proprietor,respectively;
3. for a muncipality, state,federal,or other public agency includes the chief executive officer having responsibility for the
overall operations of a principal geographic unit of the agency(e.g.,a Regional Administrator of EPA).
CERTIFICATION STATEMENT*
LegallyResponsibIc Official, submissions
certify that I am the responsible official for this facility,as described above,and hereby certify that the information contained
in this air emissions report, including attached calculations and documentation,is true,accurate and complete. (Subject to legal
enalities of up to$25,000 per occurrence and possible imprisonment as outlined in G.S.§143-215.3(a)(2))
Responsible Official's Signature Below (use blue ink): Date Signed: (P vS
Printed Name: Kev' Ham
,Signature:
This form applies to Title V facilities.If this facility is not classified as Title V,please telephone your regional office Emission
Inventory contact at once for proper forms.
Email address of Responsible Official: [e-mail]
d`\�e
Information on this Form cannot be held contidential
O�a['
COPY of RECORD Date Submitted: 6/19/2014 16:46:44 �G 1

COPY of RECORD Date Submitted: 6/19/201416:46:44
_.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
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(I I tons per hour CS-14 one bagfilter(535 sqaure CD—BP—BH1
capacity) feet of filter area),
Natural gas—fired rotary drum
ES—CD-8
coatings dryer(250,000 Btu per
j hour maximum heat input;3.45
1 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—CR7
ES—CR6 Texturizing operation for Line 2 CS D—CR7BF,
—19 area),bagfilter(4,062 square CD—CR7BF2, BF3
feet of filter.ared),bagfilter
(3,640 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
bagfilter.(air to cloth ration
ES—Coal—CC coal crusher CS-18 I), CD—Coal—CC
of4.7 to 1)
ES—K1 Wood/natural gas-fired tunnel CS-8 Two Simple cyclones(89 CD—CI,CD—C2
i 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—C1, 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 input and 20.55 tons per hour CS-15 dry limestone adsorber, CD—K3DLA
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—K4D2 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 input and 20.55 tons per hour CS-11 dry limestone adsorber, CD—K4DLA
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—CI,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
8.06 to 1) CD—SD—DC1,CD—SD—DC2,
ES—WFS—SD—CV2 Screen feed screw conveyor CS-17 ,cycicyclone(42 inches ES—WFS—SD—CYC,
in diameter),bin vent filter
(air to cloth ratio of 4.44 to CD—SD—BV 1,CD—SD—BV2
1),bin vent filter(air to cloth
ratio of 4.44 to 1),
dust collector(air to cloth
ratio of 8.17 to 1),dust
collector(air to cloth ratio of CD—SD—DCl,CD—SD—DC2,
06 to 1)
,cyclone Enclosed conveyor CS-17 8. cyclone(42 inchesES—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 of8. CD—SD—DC1,CD—SD—DC2,
i
ES—WFS—SD—CYC Cyclone CS-17 n di to 1),ameter)cyc bin n e vent n filter inches ES—WFS—SD—CYC,
n diameter),bin
(air to cloth ratio of 4.44 to CD—SD—BV1,CD—SD—BV2
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—HM hammermill CS-17 8.06 to 1),cyclone(42 inches IES—WFS—SD—CYC,
in diameter),bin vent filter CD—SD—BV1, CD—SD-1W2
(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,
ES—WFS—SD—SC1 8x8 screen CS-17 8.06 to 1),cyclone(42 inches ES—WFS—SD—CYC,
in diameter),bin vent filter
(air to cloth ratio of 4.44 to CD—SD-BV1,CD=SD—BV2
1),bin vent filter(air to cloth
ratio of 4.44 to 1),
dust collector(air to cloth
ratio of 8.17 to 1),dust
collector(air to cloth ratio of CD—SD—DC1, CD—SD—DC2,
ES—WFS—SD—SC2 8x8 screen CS-17 8.06 to 1),cyclone(42 inches 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),
ES—WFS—SD—SDS Sawdust silo CS-17 dust collector(air to cloth CD—SD—DC1 CD—SD—DC2,
ratio of 8.17 to 1),dust ES—WFS—SD-CYC,
collector(air to cloth ratio of CD—SD—BV1,CD—SD—BV2
4

8.06 to 1),cyclone(42 inches
in diameter),bin vent filter i7
(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—SH Surge hopper CS-17 8.06 to 1),cyclone(42 inches 1ES—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), -
F—C—CFBH Intersite conveyor[NSPS 40
CFR Part 60 Subpart 000]
F—CH—BC Brickhaven conveyor[NSPS 40
CFR Part 60 Subpart 000]
Impact crusher[NSPS 40 CFR
F—CH—Cl 1 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—FS1 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
Part 60 Subpart 0001
F—CH—FS4 Finishing screen[NSPS 40 CFR
Part 60 Subpart 000]
F—CH-111 Hammermill NSPS [40 CFR
Part 60 Subpart 000]
F—CH—H2 Hammermill [NSPS 40 CFR
Part 60 Subpart 000]
F—CH—PI 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 0001
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

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—TI tallings conveyor[NSPS 40
CFR Part 60 Subpart 0001
F—CH—T2 tallings conveyor[NSPS 40
CFR Part 60 Subpart 000]
F—CH-TC 1 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 95 [NSPS—
F—FCS 40 CFR Part 60 Subpart 000]
F—FS I 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—PC Primary crusher[NSPS—40
CFR Part 60 Subpart 0001
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
1
brick dryer associated with Kiln
I—ES—K2D1 2
6

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)
IES—F—CO—05 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—T5 1,000 gallon gasoline storage
tank
Package—type kiln car Two Bagfilters(97 square
IES—VS1 CS-10 feet and 297 square feet of CD—VS1,CD—VS2
vacuuming system
filter area)
Package—type kiln car Two Bagfilters(97 square
IES—VS2 CS-10 feet and 297 square feet of CD—VS1,CD—VS2.
vacuuming system -
filter area)
IES—VS3 Hi—Vac vacuum system for Kiln
3
IES—VS4 package—type kiln car
vacuuming system
IES—VS5 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)
IS-3 Screened Clay Conveying and
Handling Operation for Kiln l
7

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
III
8

I
I`
COPY of RECORD Date Submitted: 6/191201416:46:44
As entered in AERO
Facility Name: General Shale Brick,Inc.Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit : 04384
Moncure,NC 27559 County : Chatham
DAQ Region : RRO
Emission Source & Operating Scenario List- See Instructions
*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-CV I,ES-WFS-SD-CV2,
ES-WFS-SD-CV3,ES-WFS-SD=CYC,
GR21 ES-WFS-SD-HM,ES-WFS-SD-SC1, 30 Wood Fuel/Sawdust System
ES-WFS-SD-SC2,ES-WFS-SD-SDS,
ES-WFS-SD-SH
GR22 IES-VS3,IES-VS4,IES-VS5 35 Vacuum Systems-Brickhaven
G-66 ES-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
F-C-CFBH,F-FC4,F-FC5,F-FS1,
F-FS2,F-FS3,F-FS4;F-FS5,F-FS6, Primary Clay Grinding and
G-71 F-FS7,F-FS8,F-F99,F-PC,F-SS1, 31 Screening Operation
F-SS2
G-72 I-ES-K1D1,I-ES-K2D1 15 Dryers associated with Kilns 1 and
2
F-CH-BC,F-CH-C I,F-CH-CFC,
F-CH-FC,F-CH-FS1,F-CH-FS2,
F-CH-FS3,F-CH-FS4,F-CH-111,
F-CH-H2,F-CH-P1,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-T1,
F-CH-T2,F-CH-TC1,F-CH-TC2,
FCH-HFC 1,FCH-HFC2
I
G-135 ES-K4D1,ES-K4D2,ES-K4D3 29 Natural gas/propane-fired dryers l
for Kiln 4
G-143 I-F-CH-AF,I-F-CH-H,IES-CP, NONE NONE
IES-F-CH6,IES-F-CO-2,
IES-F-CO-C1,IES-F-CO-C2,
IES-F-CO-C3,IES=F-CO-C4,
IES-F-CO-05,:IES-K4F.1,IES-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,
IES—TS 18 Storage tanks
ES—BP—BM 26 Batch Mixer
- ES—BP—CS 27 Cement Silo
ES—BP—FAS 28 Flyash Silo
ES—CD-8 6 Rotary sand drum dryer(3.45 tons
per hour)
ES—CR8 NONE NONE
ES—Coal—CC 33 Coal Processing System
10 Natural gas/propane—fired kiln#3
ES—K3K (Uncontrolled)
25 10/Natural gas/propane/coal—fired
kiln#3
ES-K4K 21 Coal/Natural gas/Propane—fired
kiln#4
ES—RUMBLE 36 Rumbler tumbles blocks in a
rotating drum in order to create an
ES—SS NONE NONE
F=SGS NONE NONE
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

I
l �
COPY of RECORD Date Submitted: 6/191201416:46:44
As entered in HERO
Facility Name: General Shale Brick,Inc.Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit• 04384
Moncure,NC 27559 County.: Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2013
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 2013:
(e.g.production or fuel use):
6. Fuel Information (if fuel is used) /a 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 entr lines :
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) hate(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 2013)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
i
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an-Feb +Dec 25% 25% une—Aug. 25% �013
ept.—Nov. 25%
013 �arch—May
13 �013
U 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
2013
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAAQS Code Pollutants Method Code (Net after Factor Ef Control
Pollutantss
(Tons/Year) (See Instructions) all controls)
2013
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
J 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)
2013
_]
I .
i
12

1
COPY of RECORD Date Submitted: 6/19/201416:46:44
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 2013
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: 30500305Brick Manufacture—Material Prep;Raw Material Handling and -
Transferring
5. Throughput/units in 2013:
L_
(e.g.production or fuel use):
6. Fuel Information (If-fuel is used) r
Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
i
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—BV1 bin vent filter air to cloth ratio of4.44 to 1
5 CS-17 CD—SD—BV2 bin vent filter air to cloth ratio of 4.44 to 1
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W) -
in 0.1 feet)
13

r
Ii
P—SD—BV1 VERTICAL STACK 20 0.5 72 33.95 400 Bin vent on sawdust
-r silo
Dust Collector on
P—SD—DC2 VERTICAL STACK 20 1 72 49.76 2345 Woodfuel Sawdust
System Screens
Conveyors
P—SD—BV2 VERTICAL STACK 20 0.5 75 33.95 400 Bin Vent on Surge
Hopper
Dust Collector on
P—SD—DC1 VERTICAL STACK 20 1 72 44.56 2100 Woodfuel Sawdust
System Screens
Conveyors
1
-I
i
14

i
Operating Scenario: OS—30 Emission Source/Group ID: GR21
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks ( 52 Per Year _
)
r--
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throughput:
an—Feb +Dec 25% 250�o une—Aug. 250�o �013
ept.—Nov. 25%
013 �arch—May
13 �013
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
2013
Criteria Emissions— Emission Control A
(NAAQS) Pollutant Criteria Estimation Efficiency Emission
�Pollutants
Code Pollutants Method Code et after Factor Ef Control
(Tons/Year) (See Instructions) all controls) j
2013
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 '08
VOC VOC 08
HAP/TAP CAS Emissions Emission Control
Pollutants (In HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code y Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
.2013
i
15

i
l_
,�
COPY of RECORD Date Submitted: 6/19/201416:46:44
As entered in-HERO
Facility Name: General Shale Brick,Inc.Moncure Facility Facility ID : 1900009
300_Brick Plant Road Permit• 04384
- Moncure,NC 27559 County : Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources
i
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2013
1. Emission Source ID (from permit)or Group GR22 consisting of IES—VS3,IES—VS4,IES—VS5
Emission Source Group ID"
2. Emission Source Description: Vacuum Systems—Brickhaven
_ 3. Operating Scenario ID/Description: OS—35/Vacuum Systems—Brickhaven
4. SCC Number/Description: 30500317/13rick Manufacture—Material Prep ;Raw Material Unloading
5. Throughput/units in 2013: 2000 HR/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur ro
Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x
_._ (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 3.3 1400 Emission point for
IES—VS5
16

I
Operating Scenario: OS—35 Emission Source/Group ID: GR22
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
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
013 25/0 013 25/0 013 25/0 013 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
2013
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAA Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2013
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
HAP/TAP Emissions Emission Control
Pollutants (In CAS HAP/TAPS Estimation Emission EF Control
-
(see instructions) Method Code Efficiency Factor
Alphabetical Order) (Pounds./Year) (Net after all controls)
See Instructions
2013
17

COPY of RECORD Date Submitted: 6/19/201416:46:44
As entered in AERO
Facility Name: General Shale Brick,Inc.Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit• 04384 -
Moncure,NC 27559 County.: Chatham
i DAQ Region.:RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2013
1. Emission Source ID(from permit)or Group G-66 consisting of ES—Kl,ES—K2,ES—WD 1,2
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: 30500361/13rick Manufacture—Dryer; Sawdust Dryer:Heated With Exhaust
From Sawdust—fired Kiln
5. Throughput/units in 2013:
(e.g.production or fuel use):.
6. Fuel Information (If fuel is used) L.Sulfur %Ash Heat Content
) _T�
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 CD7C1 Sim le cyclone 89 inches in diameter
2 CS-8 CD—C2 Simple cyclone 89 inches in diameter
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ent lines):
ERP ID ERP Type Height Diameter' Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (Fj (Feet/sec) Rate(Acfm) -
Rectangle(L x W)
in 0.1 feet)
ERP for ES—K1,
EP—C I VERTICAL STACK 65 2.5 150 53 15609.78 ES—K2,and
ES—SDI
ERP for ES—K1,
EP—C2 VERTICAL STACK 65 2.5 150 53 15609.78 ES—K2,and
ES—SDI
18

- ' Operating Scenario: OS— 14
P g Emission Source/Group ID: G-66
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
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% —Aug. 25% ept.—Nov. 25%
013 013 �Om �013
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
2013
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)
2013
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP CAS Emissions Emission Control
Pollutants (In HAP/TAPS Estimation Emission
EF Control
(see instructions) Efficiency
Alphabetical Order ounds/Year Method Code Factor
P ) (P ) (Net after all controls)
See Instructions
2013 .
20

I
COPY of RECORD Date Submitted: 6/19/2014 16:46:44
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 2013
1. Emission Source ID(from permit)or Group G-69 consisting of ES—CR5,ES—CR6,ES—CR7
Emission Source Group ID
2. Emission Source Description: Texturizing Operations
3. Operating Scenario ID/Description: OS—37/Texturizing Operations _
4. SCC Number/Description: 30500397Brick Manufacture; *Other Not Classified
5. Throughput/units in 2013: 96201 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):
I
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
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional e try lines): .
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet) T
EP—CR6 HORIZONTAL STACK 20 1 72 21.2 999.02 ERP for ES—CR-6
EP—CR7 HORIZONTAL STACK 20 1 72 1 21.2 1 999.02 1 ERP for ES—CR-7
21

i
Operating Scenario: OS—37 Emission Source/Group ID: G-69
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
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% 25a/o une—Aug. 250�o �013
ept.—Nov. 25"�0
013 �arch—May
13 �013
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
2013
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAA Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2013
CO CO 08 0
NOx NOx 08 0
TSP TSP 0.17 08 99
PM10 PM10 0.17 . 08 99
PM2.5 PM2.5 0.17 08 99
S02 S02 08 0
VOC VOC 08 0
HAP/TAP Emissions Emission Control
Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) See Instructions) (Net after all controls)
2013
,I
22

COPY of RECORD Date Submitted: -6/19/201416:46:44
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 2013
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-34Nacuum System -
4. SCC Number/Description- 3 05 003 1 7/Brick Manufacture-Material Prep ;Raw Material Unloading
5. Throughput/units in 2013:
(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)
I CS-10 CD-VS1 Ba filter 97 square feet of filter area
2 CS-10 CD-VS2 Ba filter 297 square feet of filter area
ill
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ent lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP
(in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm) Description
Rectangle(L x
in 0.1 feet)
�
EPVS2 DOWNWARD-FACING VENT 1 3 72 3.3 1400 ERP for
CD-VS2
EPVS1 DOWNWARD-FACING VENT 1 3 72 3.3 1400 ERP for
CD-VS1

Operating Scenario: OS—34 Emission Source/Group ID: G-70
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
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% re .—Nov. 25%
013 013 �013
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
i
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Met after. Factor
Tons/Year See Instructions all controls
2013
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(hiAA Code Pollutants Method Code (Net afterFactor Ef Control
Pollutants •
(Tons/Year) (See Instructions) all controls)
2013
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 Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) See Instructions) et after all controls)
2013
24

COPY of RECORD Date Submitted: 6/19/2014 16:46:44
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 2013
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—PC,F—SS1,F—SS2
2. Emission Source Description: Clay Handling Equipment
3. Operating Scenario ID/Description: OS—31/Primary Clay Grinding and Screening Operation
I
4. SCC Number/Description: 30500302Brick Manufacture—Material Prep;Raw Material Grinding l
Screening
l
5. Throughput/units in 2013: 108707 TON/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) ro
Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency j
(%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) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
EP—FG FUGITIVE(NO 1 1 72 Area= 1 ERP for Fugitive
STACK) sources
25'

Operating Scenario:OS—31 Emission Source/Group ID: G-71
P g P
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
Hours per Day ( 6 ) Days per Week ( 5 ) Weeks per Year ( 48 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% arch—May 25°�° une—Aug. ° Sept.—Nov. °
013 013 013 25�O 013 25
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission Ef Control
Pollutants. Pollutants Method Code (Net after Factor
Tons/Year See Instructions all'controls
2013
i Emissions— Emission Control
Criteria Pollutant Criteria Estimation . Efficiency Emission
Po� Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2013
CO CO 08
NOx NOx 08
TSP TSP ,' 1.36 08
PM10 PM10 0.13 08
PM2.5 PM2.5 0.13 08
S02 S02 08 .
VOC VOC 08
rHAP/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
2013
G
26

COPY_ of RECORD Date Submitted: 6/19/2014 16:46:44
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 2013
1. Emission Source ID(from permit)or Group G-72 consisting of I—ES—K1D1,1—ES—K2D1
Emission Source Group ID
2. Emission Source Description: Dryers associated with materials handling equipment
3. Operating Scenario ID/Description: OS— 15/Dryers associated with Kilns 1 and 2
4. SCC Number/Description: 30500305Brick Manufacture—Material Prep;Raw Material Handling and
Transferring
5. Throughput/units in 2013:
(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).
i
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines): ; E
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
EP—FG FUGITIVE(NO 1 72 Area= 1 ERP for Fugitive
STACK) sources
I
27

' 1
Operating Scenario:OS— 15 Emission Source/Group ID: G-72
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
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% a 25% une—Aug. 25% �013
ept.—Nov. 25%
013' � rch—May
13 113
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
2013
Criteria Emissions— Emission Control
,/N C Pollutant Criteria Estimation Efficiency Emission
Ef Control
Pollutants
s Code Pollutants Method Code (Net after Factor
(TonslYear) (See Instructions) all controls)
2013
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
tHAP/TAP Emissions Emission Control
Pollutants (In CAS HAP/TAPS APS Estimation Efficiency Emission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2013
I .
i
28

COPY of RECORD _Date Submitted: 6/19/2014 16:46:44
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 2013
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: 30500351Brick Manufacture—Dryer;Brick Dryer: Heated With Waste Heat
And Supplemental Gas Burners
5. Throughput/units in 2013: 96201 TON/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content -
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
t_
9.Emission Release Point ERP i Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
EP—K4D1 VERTICAL STACK 34.78 4.92 99.95 33.79F38544.24 Brick Dryers on
Kiln 4
29

Operating Scenario: OS—29 Emission Source/Group.ID: G-135
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
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% JID13'Line—Aug. Sept.—Nov. 25%
013 �arch—May
13 2013
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
2013
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAA Code Pollutants Method Code (Net afterFactor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2013
CO CO 13.47 08
NOx NOx 4.71 08
TSP TSP 8.99 08
PM10 PM10 8.99 08
PM2.5 PM2.5 8.99 08
S02 S02 08
VOC VOC 1.44 08
Emission
HAP/TAP CAS Emissions Control
Estimation Emission
Pollutants (In (see instructions) HAP/TAPS Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) See Instructions (Net after all controls)
2013
30

COPY of RECORD Date Submitted: 6/191201416:46:44
As entered in HERO
Facility Name: General Shale Brick,Inc.Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit: 04384
Moncure,NC 27559 County : Chatham
DAQ Region :RRO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2013
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 l
2. Emission Source Description: Storage tanks
3. Operating Scenario ID/Description: OS— 18/Storage tanks
i_
4. SCC Number/Description: 39090004/Fuel Storage—Fixed Roof Tanks ;Distillate Oil(No. 2): Working
Loss
5. Throughput/units in 2013: 39923 GAL/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /°Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed in ermit
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry fines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) (Acfm)
Rectangle(L x W)
(in 0.1 feet)
EP—FG FUGITIVE(NO 1 72 Area= 1 ERP for Fugitive
STACK) sources
31

Operating Scenario: OS— 18 Emission Source/Group ID: G-144
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
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"�u une—Aug. 25% �013
ept.—Nov. 25%
013 �arch—May
13 013
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG GHG Estimation Efficient Emission
Pollutants CAS Pollutants Method Code (Net after Factor Ef Control
Tons/Year See Instructions all controls
2013
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAA Code Pollutants Method Code. (Net afterFactor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2013
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 0.12 08
HAP/TAP Emissions Emission .Control
CAS Estimation Emission
Pollutants (In (see instructions) HAP/TAPS Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) See Instructions) (Net after all controls)
2013
i
32

COPY of RECORD Date Submitted: 6/19/2014 16:46:44
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 2013
1. Emission Source ID(from permit)or ES—BP—BM
Emission Source Group ID
2. Emission Source Description: batch mixer(39.97 tons per hour capacity)
3. Operating Scenario ID/Description: OS—26Batch Mixer
4. SCC Number/Description: 31299999/Miscellaneous Machinery ; Other Not Classified
5. Throughput/units in 2013:
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS=12 CD—BP—BH1 one ba filter 535 s aure feet of filter area
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/see) hate(Acfm)
Rectangle(L x W) 1
(in 0.1 feet)
BMX VERTICAL STACK 44.95 1.312 72.05 40.02 3246.27 Batch Mixer
Ba house
33

Operating Scenario: OS—26 Emission Source/Group ID: ES—BP—BM
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
Hours per Day ( 24 ) Days per Week ( .7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
i .
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% arch—May 25% une—Aug. 25% �013
ept.—Nov. 25%
013 013 �013
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
2013
Emissions— Emission Control
Criteria
Pollutant Criteria Estimation Efficiency Emission
(NAAQS) Ef Control
Code Pollutants Method Code (Net after Factor
Pollutants
i (Tons/Year) (See Instructions) all controls)
2013
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 Method Code Efficiency Factor EF Control
- Alphabetical Order) (PoundsNear) (Net after all controls)
See Instructions
2013
34

COPY of RECORD Date Submitted: 6/19/2014 16:46:44
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 2013
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
I
4. SCC Number/Description: 31299999/Miscellaneous Machinery ; Other Not Classified
5. Throughput/units in 2013:
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) ro
Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-13 CD—BP—BV2 one bin vent filter 227 square feet of filter area
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ent 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
35

Operating Scenario: OS—27 Emission Source/Group ID: ES—BP—CS
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% 25% une—Aug. 25% Sept.—Nov. 25%
013 �arch—May
13 �013 013
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
2013
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAAQS) Code Pollutants Method Code (Met after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2013
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
r
HAP/TAP CAS Emissions Emission
Control
Pollutants (In HAP/TAPS Estimation EfficiencyEmission
(see instructions) Method Code Factor EF Control
Alphabetical Order). (Pounds/Year) (Net after all controls)
See Instructions
2013
� I
36

COPY of RECORD Date Submitted: 6/19/2014 16:46:44
As entered in AERO
Facility Name: General Shale Brick,Inca Moncure Facility Facility ID : 1900009
300 Brick Plant Road Permit.• 04384
Moncure,NC 27559 County: Chatham
DAQ Region : RRO
North Carolina Department of Environment and Natural Resources -
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2013
1. Emission Source ID (from permit)or ES—BP—FAS
Emission Source Group ID
2. Emission Source Description: flyash silo(11 tons per hour capacity)
3. Operating Scenario ID/Description: OS—28/Flyash Silo
4. SCC Number/Description: 31299999/Miscellaneous Machinery ; Other Not Classified
5. Throughput/units in 2013:
(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-14 CD—BP—BHI one ba filter 535 s aure feet of filter area
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
(in 0.1 feet)
FLY VERTICAL STACK 44.95 1.15 72 60 3739.28 Flyash Silo Bin
Vent
37

Operating Scenario: OS—28 Emission Source/Group ID: ES—BP—FAS
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For.Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% 25% une—Aug. 25% Sept.—Nov. 25%
013 �arch—May
13 013 013
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
2013
Criteria Emissions— Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission
Pollutants
Code Pollutants Method Code (Net after Factor Ef Control
(Tons/Year) (See Instructions) all controls)
2013
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP CAS Emissions Emission
Control
HAP/TAPS Estimation Emission
Pollutants (In
(see instructions) Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2013
I
38

COPY of RECORD Date Submitted: 6/19/2014 16:46:44
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 2013
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/Rota sand drum dryer 3.45 tons per hour
6/Rotary rY ( P )
4. SCC Number/Description: 30500301/Brick Manufacture—Dryer;Raw Material Drying
5. Throughput/units in 2013: 0.0735 E6FT3/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) ro
Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed in ermit
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines): _
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) (Acfm)
Rectangle(L x W)
(in 0.1 feet)
EP—FG FUGITIVE(NO 1 72 Area= 1 ERP for Fugitive
STACK sources
39

Operating Scenario: OS—6 Emission Source/Group ID: ES—CD-8
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% 25% une—Aug. 25% Sept.—Nov. 25%
013 �arch—May
13 �013 013
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 Et Control
Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2013
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAA Code Pollutants Method Code (Net after y Factor Ef Control
Pollutants (Tons/Year) (See Instructions) all controls)
2013
CO CO 0 08
NOx NOx" 0 08
_ TSP TSP 0.03 08
PM10 PM10 0.03 08
PM2.5, PM2.5 0.03 08
S02 S02 0 08
VOC VOC 0 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)
2013
Benzene 71-43-2 0.00015 08 0.0021
Formaldehyde 50-00-0 0.00551 08 0.075
Hexane,n— 110-54-3 0.1323 08 1.8
Naphthalene(Component of 91-20-3 0.00004 08 0.'00061
POMTV
Toluene 108-88-3 0.00025 08 0.0034
40
J

COPY of RECORD Date Submitted: 6/19/201416:46:44
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 2013
1. Emission Source ID(from permit)or ES—Coal—CC
Emission Source Group ID
2. Emission Source Description: coal crusher
i
3. Operating Scenario ID/Descripti6n: OS—33/Coal Processing System
4. SCC Number/Description: 39999997/Miscellaneous Industrial Processes ; Other Not Classified
5. Throughput/units in 2013: 4261 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): -
I
8. Control Device Information
Order CS—ID 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
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
P—Coal-CC VERTICAL STACKI 30 2 75 18.56 3500 One Ba filter
41

I
-- Operating Scenario: OS—33 Emission Source/Group ID:ES—Coal—CC
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
i
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 25% arch—May 25% une—Aug. 25% Sept.—Nov. 25%
013 1 013- �013 013
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
2013
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)
2013
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 9.9 1.1 BEFORE
S02 S02 08 0
VOC VOC 08 0 .
Emission
HAP/TAP Emissions Control
-- In CAS HAP/TAPS Estimation Emission
( Efficiency EF Control
Pollutants
(see instructions) Method Code y Factor
Alphabetical Order) (Pounds/Year) See Instructions) (Net after all controls)
2013
42

COPY of RECORD Date Submitted: 6/191201416:46:44
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 2013
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) -- -
i
4. SCC Number/Description: 30500311/Brick Manufacture-Curing Firing ;Curing and Firing: Gas-fired
Tunnel Kilns --
5. Throughput/units in 2013:
(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) (Feettsec) 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
43

Operating Scenario: OS— 10 Emission Source/Group ID: ES—K3K
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 250�o arch—May 250�o une—Aug. 250�0 Sept.—Nov. 25"�0
013 013 013 013
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
2013
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
��QS Code Pollutants Method Code Ef Control
Pollutantss an (Net after Factor
(Tons/Year) (See Instructions) all controls)
2013
CO CO 08
NOx NOx 08
TSP TSP . 08
VM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP Emissions Emission
CAS Estimation Control Emission
Pollutants (In (see instructions). HAP/TAPS Method Code Efficiency. Factor EF Control
Alphabetical.Order) (Pounds/Year) ctions (Net after all controls)
See Instru
2013
-
i
44

i
COPY of RECORD Date Submitted: 6/19/2014 16:46:44
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 2013
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 2013:
(e.g.production or fuel use):
6. Fuel.Information (If fuel is used) /o Sulfur ro
Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-15 CD—K3DLA dry limestone adsorber -
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional 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)
FP—K3DLA VERTICAL STACK 75.1 4.92 470.03 43.6 49734.5 dry limestone
absorber
45

Operating Scenario: OS—25 Emission Source/Group ID: ES—K3K
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
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% �013
ept.—Nov. 25%
013 013 �013
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
2013
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)
2013
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
Emission
HAP/TAP Emissions Control
CAS Estimation Emission
Pollutants (In (see instructions) HAP/TAPS Method Code Efficiency Factor: EF Control
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2013
l
_ 46

i
COPY of RECORD Date Submitted: 6/19/201416:46:44
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 2013
1. Emission Source ID (from permit)or ES—K4K
Emission Source Group ID --
2. Emission Source Description: Coal/natural gas/pr6pane—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—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
T 5. Throughput/units in 2013: 96201 O N/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-11 CD—K4DLA dry limestone adsorber
9.Emission Release Point(EPP) Information: Sources vented to more than one ERP use additional ent lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feettsec) Rate(Acfm)
Rectangle(L x W)
(in 0.1 feet)
P—K4DLA VERTICAL STACK 75.13 4.92 469 43.64 49780.13 Dry limestone -
adsorber on Kiln 4.
47

I
Operating Scenario: OS—21 Emission Source/Group ID: ES—K4K
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
Hours per Day ( 8 ) Days per Week ( 5 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu ftut.
�an—Feb +Dec 250�o arch—May 25"�u —Aug.une 250�o —Nov.Sept. 25%
013 013 �013 013
- 13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emission
Emissions— Estimation Control
GHG GHG Method Efficiency Emission
CAS y Ef Control
Pollutants
Pollutants Code (Net after Factor
(Tons/Year) (See all controls)
Instructions
2013
Emission
Criteria Emissions— Estimation Control
Pollutant Criteria Method Efficiency Emission
(NAAant Code Pollutants Code (Net after y Factor Ef Control
Pollutants
(Tons/Year) (See all controls)
Instructions
2013
CO CO 39.06 08 0
NOx NOx 39.12 08 0
TSP TSP 48.19 0.8 0
PM10 PM10 38.12 08 0
PM2.5 PM2.5 38.12 08 0
S02 S02 81.51 08 0
VOC VOC 1.15 08 0
Emission
Emissions Estimation Control
HAP/TAP CAS Emission
Pollutants (In Alphabetical Order HAP/TAPS Method Efficiency EF Control
p ) (see instructions) (Pounds/Year) Code (Net after all Factor
(See controls)
Instructions
2013
Antimony Unlisted Compounds(Specify SBC—Other 2.59743 08 0 0.000027 AFTER
Component of SBC
Arsenic Unlisted Compounds (Specify ASC—Other 8.69657 08 0
Component of ASC
Benzene 71-43-2 128.33213 08 0
Beryllium metal(unreacted) 7440-41-7 0.93969 08 0
(Component of BEC
CFC-11 richlorofluoromethane 75-69-4 1 1.34681 08 0
Cadmium Metal(elemental unreacted,
Component of CDC 7440-43-9 1.44302 08 0 0.000015 AFTER
-
48

Carbon disulfide 75-15-0 1.78741 08 0
Carbon tetrachloride 56-23-5 0.00902 08 0 -
Chlorine 7782-50-5 125.0613 08 0 0.0013 AFTER
Chloroform 67-66-3 0.00962 08 0
Chromic acid (VI)(Component of 7738-94-5 4.90625 08 0 0.000051 AFTER
So1CR6 CRC
Cobalt Unlisted Compound(Specify COC-Other 0.20202 08 0 0.0000021 AFTER
Component of COC
Di(2-eth Ihex I hthalate EHP) 117-81-7 81.1744 08 0
Dibu 1 hthalate 84-74-2 13.46814 08 0 0.00014 AFTER
Dichlorobenzene ,1,4- 106-46-7 2.03177 08 0
Dimeth 1 phthalate 131-11-3 0.07504 08 0
Ethyl benzene 100-41-4 2.90527 08 0
Ethyl chloride chloroethane 75-00-3 22.56875 08 0
Fluorides(sum of all fluoride 16984-48-8 5869.56427 08 0
compounds)
Formaldehyde 50-00-0 0.0019 08 0
Hydrogen chloride(hydrochloric acid 7647-01.-0 5599.25539 08 0 AFTER
Hydrogen fluoride(hydrofluoric acid as 7664-39-3 3668.47767 08 90 AFTER
mass of HF-Component of Fluorides
Lead Unlisted Compounds (Specify and PBC-Other 14.43015 08 0 0.00015 AFTER
Component of PBC
Manganese Unlisted Compounds(Specify Component of MNC MNC-Other 27.89829 08 0 0.00029 AFTER
Mercury,vapor(Component of HGC 7439-97-6 5.82978 08 0
Methyl bromide 74-83-9 2.30882 08 0 0.000024 AFTER
Methyl chloride 74-87-3 32.1.3113 08 0 AFTER
Methyl chloroform 71-55-6 1.16211 08 0 AFTER
Methyl ethyl ketone 78-93-3 22.89584 08 0
Methyl iodide 74-88-4 8.94669 08 0 0.000093 AFTER
Methylene chloride 75-09-2 0.07696 08 0
Naphthalene(Component of POMT 91-20-3 2.8995 08 0
Nickel metal.(Component of NIC 7440-02-0 6.92647 08 0 0.000072 AFTER
Perchloroeth lene tetrachloroeth lene 127-18-4 0.26936 08 0 0.0000028 AFTER
Phenol 108-95-2 5.32954 08 0
Phosphorus Metal,Yellow or White 7723-14-0 94.27698 08 0.
Selenium Compounds SEC 22.12623 08 0 0.00023 AFTER
Styrene 100-42-5 0.77538 08 0 --
Toluene 108-88-3 20.58701 08 0
Vinyl acetate 108-05-4 0.00962 08 0 1E-7 AFTER
X lene 1330-20-7 10.08186 08 0 --
X lene o- 95-47=6 4.94473 08 0
49

COPY of RECORD Date Submitted: 6/19/2014 16:46:44
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 2013
1. Emission Source ID(from permit)or ES—RUMBLE
Emission Source Group ID
2. Emission Source Description: rumbler system
- 3. Operating Scenario ID/Description: OS—36/Rumbler tumbles blocks in a rotating drum in order to create an
4. SCC Number/Description: 30500397/Brick Manufacture; *Other Not Classified
S. Throughput/units in 2013:
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) ro
Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Orden CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additiona entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x
(in 0.1 feet)
P—RUMBLE VERTICAL STACK 44.95 1.312 72.05 40.02 3246.27 1 Rumbler Ba house
50

Operating Scenario: OS—36 Emission Source/Group ID:
ES—RUMBLE -
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
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% rune—Aug. 25% Sept.—Nov.013 013 013 25%
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used. -
Emissions— Emission Control
GHG CAS GHG Estimation Efficiency Emission.
Pollutants Pollutants Method Code (Net after Factor Ef Control
Tons/Year See Instructions all controls
2013
Criteria Emissions— Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission
Code Pollutants Method Code et after Factor
Pollutants
Ef Control
(Tons/Year) (See Instructions) all controls)
2013
CO CO 08
NOx NOx 08 �
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC pg
HAP/TAP CAS Emissions Emission Control
Pollutants (In _ HAP/TAPS Estimation Emission
Efficiency EF Control
(see instructions) Y
Alphabetical Order) (Pounds/Year Method Code F(Net after all controls) actor
See Instructions)
2013
51

COPY of RECORD Date Submitted: 6/19/2014 16:46:44
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 2013
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: 30500397Brick Manufacture; *Other Not Classified
5. Throughput/units in 2013:
(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 in ermit
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry fines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) (Acfm)
- Rectangle(L x W)
in 0.1 feet)
FEP—FG FUGITIVE(NO 1 72 Area= 1 ERP for Fugitive
STACK) sources
i
'll
52

Operating Scenario: OS— 19 Emission Source/Group ID: IS-14
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2013)
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%
013 013 013 013
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
2013
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficient Emission
(NAAQS) Code Pollutants Method Code (Net after' Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2013
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
2013
53

Facility Total CY 2013 Emissions Summary
COPY of RECORD Date Submitted: 6/19/201416:46:44
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 2013
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 1 2013 1 2012 1 % Chan e
Criteria Pollutants
Actual Emissions Tons/Year
Pollutant CAS 2013 2012 % Change
CO CO 52.53 56.59 -7.1744146%
NOx NOx 43.83 23.15 89.33047%
PM TSP TSP 58.88 59.38 -0.84203434%
PM10 PM10 47.58 44.73 6.371568%
PM2.5 PM2.5 47.58 .53 8817.36%
S02 S02 81.51 42.03 93.932915%
_- VOC VOC 2.71 3.03 -10.561053%
Hazardous Air Pollutants HAPS and/or Toxic Air Pollutants TAPs
Actual Emissions Pounds/Year
Pollutant CAS 1 2013 1 2012 % Change
Pollutant.Group:Antimony Com ounds total mass,inc elemental SB GroupSum:2.59743
Antimony Unlisted Compounds Sec. ,
y P ( P Y
SBC-0ther 2.59743 2.18973 18.6I8736%
Component of SBC
Pollutant Group:Arsenic Compounds(total mass of elemental AS,arsine and all inorganic compounds) Group
-- Sum:8.69657
Arsenic Unlisted Compounds(Spec
Com onent of ASC) ify ASC-OtherT 8.69657 7 7:41.568 17.272732%
Pollutant Group:Beryllium compounds Total mass Group Sum:.93969
Beryllium metal(unreacted)(Component 7440-41-7 0.93969 .78815 19.227303%
of BEC
Pollutant Grou :Cadmium compounds total mass inc elemental metal Group Sum:1.44302
Cadmium Metal(elemental unreacted,
Component of CDC 7440-43-9 1:44302 1.35834 6.234077%
Pollutant Grou :Chromium VI Soluble Chromate Compounds(Component of CRC Group Sum:4.90625
Chromic acid(VI)(Component of So1CR6 7738-94-5 4.90625 4.43246 10.689102%
54

CRC
Pollutant Grou :Chromium-All/Total Inc Chromium VI cate ones metal and Others Group Sum:4.90625
Chromic acid(VI)(Component of So1CR6 7738-94-5 4.90625 4.43246 10.689102%
CRC
Pollutant Grou :Cobalt compounds Grorcm:.20202 --
Cobalt Unlisted Compound(SpecifyOC-Other 0.20202 .1688 19.6801
Component of COC
Pollutant Grou :Lead and Lead com ounds GroupSum:14.43015
Lead Unlisted Compounds(Specify and PBC-Other 14.43015 12.88974 11.950667%
Component of PBC
Pollutant Grou :Man anese compounds roup Sum:27.89829
Manganese Unlisted Compounds(Specify
Component of MNC MNC-Other 27.89829 26.64054 4.721194%
Pollutant Group:Mercury Compounds-all total mass, inc Hg Va or GroupSum:5.82978
Mercury,vapor(Component of HGC 7439-97-6 5.82978 4.94631 17,861195%
Pollutant Grou :Nickel Compounds, sum total mass inc elemental Group Sum:6.92647
Nickel metal(Component of NIC 7440-02-0 6.92647 6.02336 77F 14.99346%
Pollutant Grou :Pol c clic Organic Matter(Specific Com ounds from OA PS for TV Group Sum:2.89954
Naphthalene(Component of POMTV 91-20-3 2.89954 2.42008 19.811743%
Acrylonitrile 107-13-1 0.0 .1318 -100.0%
Benzene 71-43-2 128.33228 111.08493 15.526269%
CFC-II Trichlorofluoromethane 75-69-4 1.34681 1.13694 18.459196%
Carbon disulfide 75-15-0 1.78741 1.62487 10.003266%
Carbon tetrachloride 56-23-5 0.00902 .01068 -15.543076%
Chlorine 7782-50-5 125.0613 104.4966 19.679785%
Chloroform 67-66-3 0.00962 .01068 -9.925099%
Di 2-eth lhex 1 hthalate DEHP 117-81-7 81.1744 68.77118 18.035494%
Dibut 1 hthalate 84-74-2 13.46814 11.36447 18.510939%
Dichlorobenzene , 1,4- 106-46-7 2.03177 1.7 19.515879%
Dimeth 1 phthalate 131-11-3 0.07504 .06272 19.64285%
Ethyl benzene 100-41-4 2.90527 2.49937 16.240091%
Ethyl chloride chloroethane 75-00-3 22.56875 18.9 19.411379%
Fluorides sum of all fluoride compounds) 16984-48-8 5869.5645 7459.816 -21.31757%
Formaldehyde 50-00-0 0.00741 22.40735 -99.966934%
Hexane,n- 110-54-3 0.1323 .1764 -25.000002%
Hydrogen chloride(hydrochloric acid 7647-01-0 5599.2554 5855.59 4.377603%
Hydrogen fluoride(hydrofluoric acid as 7664-39-3 3668.4778 4659.31 -21.265644%
mass of HF-Component of Fluorides
Methyl bromide 74-83-9 2.30882 2.2344 3.330647%
Methyl chloride 74-87-3 32.13113 36.5118 11.997953%
Methyl chloroform 71-55-6 1.16211 .97461 19.238464%
Methyl ethyl ketone 78-93-3 22.89584 20.62614 11.003993%
Methyl.iodide 74-88-4 8.94669 9.14041 -2.1193886%
Methylene chloride 75-09-2 0.07696 .49439 -84.43334%
Perchloroeth lene tetrachloroeth lene 127-18-4 0.26936 .22771 18.290815%
Phenol 108-95-2 5.32954 5.1437 3.6129565%
Phosphorus Metal Yellow or White 7723-14-0 94.27698 82.61535 14.115571%
Selenium Compounds SEC 22.12623 18.8139 17.60576%
Styrene 100-42=5 0.77538 .67714 14.5080805%
55

Toluene 108-88-3 20.58726 20.18324 2.001752%
Vinyl acetate 108-05-4 0.00962 .00936 2.777779%
X lene 1330-20-7 10.08186 12.85181 —21.553001%
X lene, o— 95-47-6 4.94473 4.18064 18.276855%
56

COPY of RECORD Date Submitted: 6/19/2014 16:46:44
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:
i
57

SECTION 2
2013 SUPPORTING EMISSION CALCULATIONS
General Shale Brick, Inc. -Moncure, NC Facility I CY 2013 Emissions Inventory
Trinity Consultants

Title: 2013 Air Emission Inventory
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility 1D#: 1900009
Critical Parameters Table
Parameter I Value
Combustion Sources-Ca Re Fear
Actual Brick Production 0 tons per year
Actual Sawdust Usage 0 tPy
Combustion Sources-Brickhaven-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 () t v
Combustion Sources-Brickhaven-Kiln 4 and Associated Drvers
Actual Brick Production(Natural Vas) U tp
Actual Brick Production Coal&NG) 96,201 tpy
Acutal Gas Usage 62,697,260 scf/ r
Actual Coal Usage 4,261 t v
Wood Waste Svstem-Ca e Fear
Number of Cyclones I 1
Sawdust preparation I I) hr cr
Clay flandling Operations
Actual Raw Material Processed 108,707 tpy
Hours of operations 1.750 hr/yr
Intersite Conveyor
Process Through xit I I US.7U7 t n
Sand Drver-Ca 1e Fear
Hours of o ierrtions ;00 lu/vr
Texturing O erations
Actual Brick Production 90,201 tPy
Baghouse Efficiency 99.8%
Hours of operation-Brick Haven 2,000 hr/yr
Hours of operations-Cape Fear 0 hr/vr
Vacuum Systems
Hours of operations-Cape Fear VS 1 0 hr/ r
Hours of operations-Brick Haven VS2 hr/ r
Hours of operations-Brick Haven(VS3)-Kiln 3 2,000 hr/yr
Houfs--o ations-Brick I laven4VS4&V-S5) 0 lif/vr
Flvash silo
Flvash silo"I'hrou 11 xn
Cement Silo
Cement silo I lirou<h tut t)%
Mixer Loading
Mixer f.oadin, Through nil t
Aggregate Iloading
Aggregate Loading Throughput t��
Rumbler
Hours ofo Aerations hr%r
1,uel Usage
Diesel Tank 27,915gal/yr
Gasoline Tank 2,743gal/yr
Waste Oil Tank 500 al/ r
Motor Oil Tank 165gal/yr
Brick Oil Tank 3,000 al/ r
Gear Oil Tank 600gal/yr
Reference:
Information Provided by Warren Paschal,General Shale Brick,Inc.,June 2014
Support Calculations File: El 2013-Moncure.xlsx
Printed 6/19/2014 Page 1 of 35 Sheet: Input

Title: _ 2013 Air Emission Inventory
Source ID fh ES-KI,ES-K2,ES-SDI
Facility: General Shale Brick,Inc
Location: Moncure,NC _
Facility ID N 1900009
Brick Processing System-Capelear
Description: After the wet clay is formed and coated it passes through the brick dryer and the kiln. The kiln is
sawdust fired. Combustion products and heat generated by the kiln are vented to the drum dryer
which dries the sawdust. From the drum dryer the exhaust is vented to the atmosphere. However,not
all of the heat from the kiln is vented to the wood dryer. Instead,some evaporative heat is routed to
the brick dryers and vented to atmosphere. -
Approach: The AP-42 Section 11.3 is used to estimate the emissions from these emission units, except for
Fluoride and hydrogen fluoride factors developed from a GSB test at Moncure.
i
'x ,.,e€„t;Paraiiiete� _.✓<.:a..,.a�.�..ri'�;�� .�„* �Yalue3F
Actual Brick Production 0 tpy
Actual Sawdust Usage - tpy
EMISSION CALCULATIONS
Emissions are calculated by the following equation: '
Yearly Emissions
Emission Factor(lb/tons brick)•Brick Production(tpy)=Emissions(lb/yr)
Emissions(lb/yr)/2000lb/ton=Emissions(tpy)
Note:The Formaldehyde emissions are multiplied by the wood usage instead of bricks usage.
Support Calculations Fie:E12073-Moncurex1s:
Printed:6/192014 Page 2 o135 _ Sheet Brick-CF(G-66)

Source: ES-Kl,ES-K2,ES-SD1 Sawdust Kilns 1&2 and sawdust dryer
Actual Annual Process Throughput: - Tons/yr
Brick Kiln Fuel: Wood
3 Emrsslon Fa tor'(Ib/fongAnnual Ann"ual
' 1 TAP NO CASNO 3 3 mrsston Rate Emrss on Rate
x fired bucks produced) _,
P.ollutant�. ,,. s (Ibs%yr) (1PY)
PM 0.675 d -W 44 0 0.00
PM-10 0.675 d `k� 0 0.00
PM 2.5 0.675 d 0 0.00
S02 p, 7 1F 0 0.00
NOx 0.37 °d _ 0 0.00
VOC 0.18 °` 0 0.00
CO ,0:344 d 0 0.00
1,4-dichlorobenzene 36 106.46-7 0.00E+00 0.00E+00
2-butanone(MEK) 70. 78-93-3 2.20E-04 ab 0.00E+00 0.00E+00
2-methylphenol(cresol) 35 9548-7 2.40E-09 °b 0A0E+00 0.00E+00
Acrylonitrile 4 107-13-1 1.90E-05 ab 0.00E+00 0.00E+00
Antimony HAP ANTIMONYCPDS 2.80E-06 ° 0.00E+00 0.00E+00
I '
Arsenic 9 ARSENICCPDS 2.10E-05 0.00E+00 0.00E+00
Benzene 12 7143-2 5.60E-04 n6 0.00E+00 0.00E+00
Beryllium 16 BERYLCPDS 3.10E-07 °' 0.00E+00 0.00E+00
Bis(2-ethylhexyl)phthalate;di(2-
ethylhexyl)phthalate 39 117-87-7 1.40E-04 ab 0.00E+00 0.00E+00
Bromomethane(Methyl Bromide) HAP' 74-83-9 4.40E-05 ab 0.00E+00 0.00E+00
Cadmium 23 CADMIUMCPDS 2.20E-05 °' 0.00E+00 0.00E+00
Carbon Disulfide 27 75-15-0 1.80E-05 ab 0.00E+00 0.00E+00
Carbon tetrachloride 28 56-23-5 3.80E-07 ab 0.00E+00 0.00E+00
Chlorine 29 0.00E+00 0.00E+00
Chloroethane(Ethyl Choroethane) HAP 75-00-3 0.00E+00 0.00E+00
Chloroform 31 67-66-3 3.80E-07 a6 0.00E+00 0.00E+00
Chloromethane(Methlyl Chloride) HAP 74-87-3 0.0014 a6 0.00E+00 0.00E+00
Chromium(expressed as chromic
acid) HAP CROMCPDS 4.80E-05 °a 0.00E+00 0.00E+00
Cobalt HAP 7440-484 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 v6 0.00E+00 0.00E+00
Di-n-butylphthalate HAP 84-74-2. 1.60E-05 ab 0.00E+00 0.00E+00
Ethylbenzene HAP 100-41-4 1.00E-05 ab 0.00E+00 0.00E+00
Fluorine 50 0.00E+00 0.00E+00
Formaldehyde 51 50-00-0 6.63E-03 0.00 0.00E+00
i
Hydrazine HAP 0.00E+00 0.00E+00
Hydrogen Fluoride 59 7664-39-3 0.23 h 0.00E+00
HCl 57 7647-01-0 0.17 of - 0.00E+00 .
Hydrogen Sulfide 60 7783-064 0.00E+00 0.00E+00
lodomethane(Methyl Iodide) HAP 74-884 2.40E-04 ab 0.00E+00 0.00E+00
Lead HAP LEADCPDS 120E-04 as 0.00E+00 0.00E+00
M-/p-Xylene HAP 108-38-3/10642-3 2.90E-05 ah 0.00E+00 0.00E+00
Manganese 62 MANGCPDS' 4.80E-04 a 0.00E+00 0.00E+00
I I I-Trichloroethane
(methylchloroform) 68 71-55-6 5.20E-07 °b 0.00E+00 0.00E+00
Methylene Chloride 69 74-87-3 6.20E-05 I°b 0.00E+00 0.00E+00
1 Mercury 66 MERCCPDS 1.10E-05 0-00E+00 0.00E+00
Naphthalene HAP' 91-20-3 2.40E-09 lab 0.00E+00 0.00E+00
Nickel 75 NICKCPDS 3.40E-05 as 0.00E+00 0.00E+00
o-Xylene HAP 9547-6 7.30E-06 °b 0.00E+00 0.00E+00
Ozone 0.00E+00 0.00E+00
Perch loroethylene
(Tetrachloroethene) 81 .127-184 3.80E-07 lah 0.00E+00 0.00E+00
Phenol 82 108-95-2 1.00E-04 I°h 0.00E+00 0.00E+00
Phosphine 71 0.00E+00 0.00E+00
Phosphorus HAP 1 7723-14-0 5.50E-04 as 0.00E+00 0.00E+00
Support Calculations File:EI 2013-Monwrexl-
Printed:61192014 Page 3 of 35 Sheet:Brick-CF(G-66) -

Selenium HAP SEC 4.70E-05 0.00E+00 0.00E+00 --
Styrene 91 10042-5 4.20E-06 ab 0.00E+00 0.00E+00
Toluene 97 108-88-3 4.30E-04 ab 0.00E+00 0.00E+00
Total Fluorides(including HF) 50 1698448-8 b O, 0.00 0.00E+00
Trichlorofluoromethane 100 75-69-4 1.00E-06 ab 0.00E+00 0.00E+00
Vinyl acetate HAP 108-05-4 1.90E-07 a6 0.00E+00 0.00E+00
Xylene 104 1330-20-7 3.63E-05 0.00E+00 0.00E+00
a Emission factors from AP42,Section 11.3,8/97
as Table 11.3-7 for sawdust fired kilns and sawdust dryer.
ab Table 11.3-6 for sawdust fired kilns and sawdust dryer.
Table 11.3-2 for sawdust fired kiln and sawdust dryer.
ad Table 11.3-3 for sawdust fired kilns.
a` Table 11.3-5 for sawdust fired kilns and sawdust dryer.
ar Table 11.34 for uncontrolled sawdust or natural gas fired tunnel kiln.
b Based on General Shale Brick Moncure Facility Stack Testing-DAQ requires TF=Fluorides of 0.04 lb/ton+HF of 0.23 lb/ton)
Emission factor provided by NCDENR,the emission factor basis is pound of emissions/tons of wood;
therefore,the factor is multiplied by the wood used.
Sawdust Usage-from input Table= tpy
d Testing was 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 Ratfrt Emission
! Pollutant „__ s r Tested(lb/hi), "r tfao' (Ib/ton)
PIv1` 15.05 0.675
°►/-J`5 ✓I'IGP?j�`" �' �Q CO 7.68 0.344
s: LuJ'd� lJutG "� �elZi:l�Ei,/�-eB
4 ¢2C" S02 data was from a September 27,2004 engineering test on Kiln 3 with
!I 3 Z awJ `/3�• a a process weight rate of. 19.58 tons/hr
7. S ry
- � .Highest Run Eiiiissions Emission�
Pollutant,; .v. ,.,� Rate Testeyt,pb%hr)tyFactor(16/ton)
SOZ. 0.56 0.029
S02 factor for wood combustion AP42-Section 1.6 0.025 lb/MMBtu
MMBtu for wood=Tons wood fired •2000 lb/ton•8000 Btullb
MMBtu for wood= 0 MMBtu --
S02 Emissions=Tested lb/ton•Actual Production ton/yr+Wood Combustion Factor Ib/Mmbtu•MMBtuyr fired
S02 Emissions= - Ibs/yr
-
ful Z00a
Support calculations File:El 2013-Moncure-Am
Printed:6119=14 Page 4 of 35 Sheet Brick-CF(G-66)

Title: 2013 Air Emission Inventory
Source ID#: ES-K3K
Facility: General Shale Brick,Inc
Location: Moncure,NC
Facility ID q: 1900009
Brick Processing System-Brick Haven-Kiln 3
Source: ES-K3K Kiln 3
Actual Brick Production: 0 Tons/yr
Coal Fired 0 Tons/yr
Brick Kiln Fuel: Coal/NG
60% Coal
.40%Natural Gas
Control Eff.of HF 90% (NESHAP Requirement)
Uncontrolled s`r
Em sslo Emnsstonrr
TO NO ° "' yRef Factor:for Tested Total yr
Factor"for Coal N -
Natural Gas Em�sston Annual Annuals
P,ollut
m ant; `from AP 42; b F
fro AP 42 Ref Factors zRef Em�sslons Emissrons
w5
;..' =Ib/ton)
PM 4.12E-01 s 0.00 0.00E+00
PM-10 2.03E-01 s 0.00 0.00E+00
PM-2.5 2.03E-01 s 0.00 0.00E+00
S02 38.000 f 2.86E-02 d 0.00 0-00E+00
NOx FIN 8.13E-01 0.00 O:00E+00
VOC 2.40E-02 ad 2.40E-02 ad 0.00 0.00E+00
CO 8.00E-01 ab 0.83 ai 0.00 0.00E+00
Chlorine 29 1.30E-03 of 0.00 0.00E+00
HF 59 3.81 E-01 d 0.00 0.00E+00
HCl 57 5.82E-02 d 0.000 0.00E+00
III-Trichloroethane 68 1.70E-05 ac 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 ae 0.00E+00 0.00E+00
1,4-dichlorobenzene 36 3.20E-06 ac 4.80E-05 of 0.00E+00 0.00E+00
2-butanone(MEK) 70. 2.50E-04 de 2.20E-04 of 0.00E+00 0.00E+00
I
2-Hexanone NA 9-40E-07 ae 8.50E-05 al 0.00E+00 0.00E+00
2-methylphenol(cresol) 35 2.20E-06 9e 0.00E+00 0.00E+00
2-methylnaphthalene NA 1.70E-06 ae 5.70E-05 of O.00E+00 0.00E+00
Antimony NA 2.70E-05 ah 0.00E+00 0.00E+00
Acetone NA 6.80E-04 ae 1.70E-03 of 0.00E+00 0.00E+00
Arsenic 9 1.30E-04 as 3.10E-05 ah 0.00E+00 0.00E+00
Benzene 12 2.90E-04 ae 2.90E-03 ae '0.00E+00 0.00E+00
Benzoic Acid 2.50E-04 ac 0.00E+00 0.00E+00
Beryllium 16 1-60E-05 as 4.20E-07 ah 0.00E+60 0-00E+00
Bis(2-ethylhexyl)phthalate;di(2- 39 7.30E-05 ae 2.00E-03 'f 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 ae 1.80E-05 ar 0.00E+00 0.00E+00
Cadmium 23 1.50E-05 ah 0.00E+00 0.00E+00
Carbon Disulfide 27 2.30E-06 ae 4.30E-05 of 0.00E+00 0.00E+00
Support Calculations File: El 2013-Moncure.xlsx
Printed:6/79/2014 Page 5 of 35 Sheet: Brick-BH(ES-K3K_G12)NG&Coal

Carbon tetrachloride 28 1.00E-07 0.00E+00 0.00E+00
Chlorobenzene HAP 2.10E-05 ae 0.00E+00 0.00E+00
Chloroethane(Ethyl HAP 1.10E-05 ae 5.70E-04 of 0.00E+00 0.00E+00 -
Chloroform 31 1.00E-07 ac 0.00E+00 0.00E+00
Chloromethane(Methyl HAP 1.10E-04 ae 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 ae 0.00E+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 120E-05 - 0.00E+00 0.00E+00
Ethylbenzene HAP 2.10E-05 ae 4.40E-05 of 0.00E+00 0.00E+00
Formaldehyde 51 7-50E-02 b 0.00E+00 0.00E+00
lodomethane(Methyl Iodide) HAP 9.30E-05 of 0.00E+00 0.00E+00
lsophorone HAP 3.00E-05 ac 0.00E+00 0.00E+00
Lead NA 1.50E-04 ah 0.00E+00 0.00E+00
M-/p-Xylene HAP 1.30E-04 ac 6-70E-05 of 0.00E+00 0.00E+00
Manganese 62 2.90E-04 as 2.90E-04 ah 0.00E+00 0.00E+00
Mercury 66 9.60E-05 as 7-50E-06 ah 0.00E+00 0.00E+00
Naphthalene HAP 6.90E-06 ae 6.50E-05 ae 0.00E+00 0.00E+00
Nickel 75 7.20E-05 ah 0.00E+00 0.00E+00
o-Xylene HAP 4.70E-05 ae 5.80E-05 de 0.00E+00 0.00E+00
Perchloroethylene of 0.00E+00 0.00E+00
(Tetrachloroethene) 81 2.80E-06
Phenol 82 3.50E-05 8.60E-05 ae 0.00E+00 0.00E+00
Phosphorus HAP 9.80E-04 as 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 ae 0.00E+00 0.00E+00
Toluene 97 2.50E-04 ae 1.60E-04 ae 0.00E+00 0.00E+00
Total Fluorides 50 6.10E-01 a 0.00E+00 0.00E+00
Trichlorofluoromethane 100 1.40E-05 ae 0.00E+00 0.00E+00
Vinyl acetate HAP 1.00E-07 ae 0.00E+00 .0.00E+00
'Emission factors from AP42,Section 11.3,8/97
as Table 11.3-1 for uncontrolled coal-fired and natural gas-fired kilns.
PM for condensible PM= 0.59 lb/ton
abTable 11.3-3 for coal-fired and natural gas-fired kilns.
"Table 11.34 for coal-fired and natural gas-fired kilns
i
ad Table 11.3-5 for brick kilns.'Table 11.3-6 for coal-fired kilns.
"'Table 11.3-6 for natural gas-fired kilns
"Table I L3-7 for coal-fired kilns.
A Table 11.3-7 for natural gas-fired kilns.
ai Factor is from AP42 Background Document testing at -
I
Marseilles Brick which has the same type of kiln
I
a3 Soluble Chromate Compounds is the regulated NC TAP -
b Emission factors from AP42,Section 1.4,7/98. The emissions factor in in Ib/mmft3 of gas. The actual gas rate: -
Formaldehyde Emission Factor=
0.0 MMBtu/hr/1020 Btu/113*1 C6 Btu/MMBtu/I0^(ft3/MMft3)= 0.0000 mmft3/hr
` Using AP-42 background information,assume that total fluorides emission factor is 60%of the HF emission factor
Also DAQ requires that total fluorides include HF,therefore TF=fluorides+HF(lb/yr)
.TF=((0.381 lb/ton*0.60)+0.381 lb/ton)*Brick Production ton/yr*(I -CE)
°Testing was performed on Kiln 4 on February 10,2006. Emissions Factors are as follows:
Process weight.rate during test 19.93 ton/if
Support calculations File: El 2013-Moncure.xlsx
Printed:611912014 Page 6 of 35 Sheet: Brick-BH(ES-K3K G12)NG&Coal

i
HighesfRun
Emissions Rate. �cEmisstonFacto�
Pollutant. Tested(Ib/hr)
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
**S02 data was from a September 27,2004 engineering test on Kiln 3 with
a process weight rate of: 19.58 tons/hr
`Test Results of Tested Highest run from Kiln and Dryer from Nov.11,2004 Indiana stack test=
NOx Emission Factor= 9.67 Ib/hr / 11.89 ton/hr
NOx Emission Factor= 0.813 lb/ton
r AP42 coal combustion
Ap42 Emission Factor:Section 1.1 Table 1.1-3 38S lb/ton coal fired
Sulfur Content of Fuel 1.000%
S02 EF= 38 lb/ton coal fired
s A coal fired kiln with a DLA was tested at a GSB site in VA.A total of three(3)test runs for Particulate Matter was conducted on February 23,2005
and a total of three(3)test runs for Particulate<10 microns was conducted on February 24,2005.
Highest Run Production Data " 29,624 lbs of brick/hr
Emission Factors are as follows:
Average re s� r.,
Emrsstons Rate w
'` Entssn Factor
Pollutant � Tested(16)ttr)„i: +(lb/top) s
PM -6.1 0.412
PM to 3 0.203
PM2.5 3 0.203
I
Support Calculations File: El 2013-Moncure.xlsx
Printed:6/19l2014 Page 7 of 35 Sheet: Brick-BH(ES-K3K G12)NG&Coal

Title: 2013 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
'1014"Adbual"'
EllhissI6-fi Jpactqft',*:'(lb/ton'.fiked-'.br'ic'. -.,pro ueed),"',� � Rate Qjy rf,'
J
PM 0.187 ac 0.00 0.00
PM-10 0.187 ac 0.00 0.00
PM-2.5 0.187 ac 0.00 0.00
S02 0.00
NOx 0.098 as 0.00 0.00
VOC 0.03 ab 0.00 0.00
CO 031 as 0.00 0.00
Formaldehyde 1.55E-01 lb
a Emission factors from AP-42,Section 11.3, 8/97
as Table 11.3-3 for brick dryer with supplemental gas burner
A
Table 11.3-5 for brick dryer.
ac Table 11.3-1 for brick dryer.
b The formaldehyde emissions from the dryer are included in the kiln calculation.
Support Calculations File: El 2013-Monc'ure.xlsx
Printed:6119/2014 Page 8ol'35 Sheet: Brick-BI-1(ES-K3K—G12)(total)

` 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/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 ton/hr
> ' a � es t Hf h Run y
`� �� � s�<,�rEt�►tsstons�Rate � ,.�EmtsstpnFactor
HF* 7.6 0.381
HCI* 1.16 0.058
PM 2.25 0.113
PM filterable 2.25 0.113
S02** 0.56 0.029
*Total Fluorides are 60%of HE
**S02 data was from a September 27,2004 engineering test on Kiln 3 with
a process weight rate of 19.58 tons/hr
`Test.Results of Tested Highest run from Kiln and Dryer from Nov.11,2004 Indiana stack test=
NOx Emission Factor= 9.67 lb/hr / 11.89 ton/hr
NOx Emission Factor= 0.813 lb/ton
f AP-42 coal combustion
Ap42 Emission Factor:Section 1.1 Table 1.1-3 38S lb/ton coal fired
j
Sulfur Content of Fuel 1.000%
SO2 EF= 38 lb/ton coal fired
I
s A coal fired kiln with a DLA was tested at a GSB site in VA.A total of three(3)test runs for Particulate Matter was conducted on February 23,2005
and a total of three(3)test runs for Particulate<10 microns was conducted on February 24,2005.
Highest Run Production Data 29,624 Ibs of brick/hr
r
! Emission Factors are as follows:
a „zAverage E v
{ Em�sstons Rate Emrssron Factor
Pollutant,• �' ,Tested(ltf/h•j„, ,, � � (Iti/ton) ,
PM 6.1 0.412
PM, 3 0.203
PMZ.$ 3 0.203
i I
i
Support Calculations File: El 2013-Moncure.xlsx
Printed:6/16/2014 Page 11 of 35 Sheet: Brick-BH(ES-K4K G12)NG&Coal .

Title: 2013 Air Emission Inventory. r
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: 96,201 Tons/yr --
Brick Dryer Fuel: NG/Propane
--
3 } n
�a x s ,201Anu al
Em>tss>lon Factor jIb/ton lired201X Em>tsston
Pollutants b4c: produced) Rate Ib/yr) ate�TPY)
PM 0.187� ad 17989.59 8.99
PM-10 0.187 ad 17989.59 8.99
PM-2.5 0.187 ad 17989.59 8.99
SO2
NOX 0.098 as 9427.70 4.71
vOC 0.03 ab 2886.03 1.44
CO 1G.2r ao 0.31 2693&.28—
Formaldehyde 1.55E-01
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.
CIO
NO
@�� sI? 2�� ?�S� 6.P�0°�, �$a '"�/T�'d✓�� /I2.' 7 t`?�OGdv1�
Printed:6/19l2014 Support Calculations He: El 2013-Moncure.xlsx
Page 12 of 35 Sheet: Brick-BH(ES-K4K G12)(total)

_ - Title: 2013 Air Emission Inventory
Source ID 0: ES-KI,ES-K2,ES-SDI,ES-K2K,ES-K41C,ES-K4D1,ES-K4D2,ES-K4D3
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility 1D 4: 1900009
V,
Wood Rlns& a wfis <s : s s r t z ,g# :rw a .s.0
x(> 3 CAS Number~ es ITAPMAP�' pryeal&2 ICdo 3 K1ln�Kiln 3 Dryer Bnckhaveo3 Kiln 4 IUIn x Kd a )Bnekhdven d 4 ~Total ,
:,:a ,„�,31 14 N ��PY) z3,(tPY) (1PY),, Total,(tonlyr) (tPYS„` 1>7;�r(SPY) Totaly(}Goslyr� Toul(Iblyr) 4TPY,y.".
PM 0.00E+00 0.00E+00 'O.DOE+00 4.82E+01 8.99E+00 57.18 1.14E+05 57.18
PM-10 0.00E+00 0.00E+00 0.00E+00 3.81E+01 8.99E+00 47.12 9.42E+04 47.12
PM 2.5 0.00E+00 0.00E+00 0.00E+00 3.81E+01 8.99E+0D 47.12 9.42E+04 47.12
S02 0.00E+00 0.00E+00 0.00E+00 8.15E+01 0.00E+00 91.51 1.63E+05 91.51
NO-, 0.00E+00 0.00E+00 0.10E+00 3.91E+0l 4.71E+00 43.83 8.77E+04 43.83
VOC 0.00E+00 1 0.00E+00 0.00E+00 1.15E+00 1.44E+10 2.60 5.19E+13 _ 2.60
0.00E+00 0.00E+00 0.00E+00 3.91E+01 1.35E+01 52.53 1.05E+05 52.53
Poundslyr
ivDod Kilns&
_ , 'c y y c #T Dryers 1&Yf 'IUIn 31U1n K11n 3 Dryer.Bncldlavea�n�3, I410 i Kdn Dryer Bnckhaven 4 �r a e Total
uz.�..ha`.c..-.k:�-(Iblyr),, (Ib/yr)�,a :c7ota�(l�/yr/ ; (Ib/yr).
1,4-dlchlorobenzene 36 10646-7 0.00E+00 .0.00E+0O 0.00E+00 2.03E+00 2.03E+00 2.03E+00 1.02E-03
2-butanone(MEK) 70 78-93-3 0.00E+00 0.00E+00 0.00E+00 2.29E+01 2.29E+01.. 2.29E+01 1.14E-02
2-me I henol(cresol) 35 9548-7 0.00E+00 0.00E+00 0.00E+00 2.12E-01 2.12E-01 2.12E-01 1.06E-04
A-lonitrile 4 107-13-1 0.00E+00 O.00E400 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00
Amicnony HAP ANTIMONYCPDS O.00E400 0.00E+00 0.00E+00 2.60E+00 2.60E+0O 2.60E+00 1.30E-03
Arsenic 9 ARSENICCPDS 0.00E+00 0.00E+00 O.00E+00 8.70E+00 8.70E+00 8.70E+00 4.35E-03
Benzene 12 7143-2 O.00E+00 0.00E+00 0.00E+00 128E+02 1.28E+02 1.28E+02 6.42E-02
_ Bcryllitun 16 BERYLCPDS 0.00E+00 O.00E400 0.00E+00 9.40E-01 9.40E-01 9.40E-01 4.70E-04
Bis(2-elh),lhexyl)ph1hala1e.,di(2- 117-87-7 0.00E+00
.cdn,lh 1 hthalale 39 0.00E+00 0.00E+00 8.12E+01 8.12E+01 8.12E+01 4.06E-02
Bromomethane(Methyl Bromide) HAP 74-83-9 O.00E+00 O.00E+00 0.00E+00 2.31E+00 2.31E+00 2.31E+00 I.I5E-03
Cadmium 23 CADMIUMCPDS O.00E+00 O.00E+00 O.00E+00 1.44E+00 1.44E+00 144E+00 7.22E-04
Carbon Disulfide 27 75-I5-0 O.00E+00 O.00E+00 0.00E+00 1.79E+00 1.79E+00 1.79E+00 8.94E-04
- Carbon tetrachloride 28 56-23-5 O.00E+00 0.00E+00 O.DOE+00 9.62E-03 9.62E-03' 9.62E-03 4.81E-06
Chlorine 29 0.00E+00 0.00E+00 0.00E+00 1.25E+02 1.25E+02 1.25E+02 6.25E-02
Chlonxthanc Ethyl Chorocthane) HAP 75-00-3 0.00E+00 0.00E+00 O.00E+00 2.26E+01 2.26E+01 2.26E+01 1.13E-02
Chloroform 31 67-66.3 0.00E+00 0.00E+10 0.00E+00 9.62E-03 9.62E-03 9.62E-03 4.81E-06
Chloromethace MethlyChloride) HAP 74-97-3 0.00E+00 O.00E+OO 0.00E+00 3.21E+01 3.21E+01 3.21E+0I 1.61E-02
Chromium e<resscd as chromic acid HAP CROMCPDS 0.00E+0p 0.00E+10 0.00E+00 4.91E+00 4.91E+00 4.91E+00 2.45E-03
Cobalt - HAP 7440484 O.00E+00 0.00E+00 O.00E+00 2.02E-01 2.02E-01 2.02E-01 LOIE-04
Dielh 4 hlhalalc HAP 84-66-2 0.00E+00 0.00E+00 0.00E+00 9.32E+00 9.32E+00 9.32E+00 4.66E-03
Dinreth I hthalate HAP 131-11-3 O.00E+00 0.00E+00 O.ODE+00 750E-02 7.50E-02 7.50E-02 3.75E-05
- Di-n-butylphthalate HAP 84-74-2 O.00E+00 0.00E+00 O.00E+00 1.35E+01 1.35E+01 1.35E+01 6.73E-03
Ethvlbcnzene HAP 100414 O.00E+00 O.00E+00 O.00E+00 2.91E+00 2.91E+00 2.91E+00 1.45E-03
Fluorine 50 O.00E+00 O.00E+00 O.00E+00 O.00E+00 0.00E+00 O.00E+00 0.00E+00
Formaldehyde 51 50-00-0 O.00E+00 0.00E+00 O.00E+00 1.90E-03 1.90E-03 1.90E-03 9.52E-07
Hydrazine HAP 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 O.00E+00 0.00E+00
HF 59 7664-39-3 O.00E+00 0.00E+0(1 0.00E+00 3.67E+03 3.67E+03 3.67E+03 1.83E+00
HCI 57 7647-01-0 0.00E+00 11.00E+00 0.00E+00 5.60E+03 5.60E+03 5.60E+03 2.80E+00
Hydrogen Sulfide 60 7783-064 O.00E+00 0.00E+00 0.00E+00 O.00E+00 0.00E+00 0.00E+0() O.00E+00
lodomethane(Melhvl Iodide) HAP 74-884 0.00E+00 0.00E+00 0.00E+00 8.95E+00 8.95E+00 8.95E+00 4.47E-03
Lead HAP LEADCPDS 0.00E+00 O.00E+00 0.00E+00 1.44E+01 1.44E+01 1.44E+01 7.22E-03
Mil X lent HAP 108-38-3/10642-3 0.00E+00 0.00E+00 O.00E+00 LOIE+01 1.01E+01 LOIE+01 5.04E-03
Manganese 62 MANGCPDS 11.00E+0(1 O.00E+00 O.00E400 2.79E+OI 2.79E+01 2.79E+01 1.39E-02
III-Trichlomethanc 68 71-55-6 0.00E+1(1
(methvlchlorofonn 0.00E+1lO 0.00E+00 1.16E+00 1.16E+00 1.16E+00 5.81E-04
Methvlene Chloride 69 74.87.3 O.00E+00 0.00E+00 O.00E+00 7.70E-02 7.70E-02 7.70E-02 3.85E-05
Mercury 66 MERCCPDS O.00E+00 O.ODE+00- O.00E+00 5.83E+00 5.83E+00 5.83E+00 2.91E-03
Naphthalene HAP 91-20-3 0.00E+00 0.00E+00 0.00E+00 2.90E+00 2.90E+00 290E+0D 1.45E-03
Nickel 75 NICKCPDS O.00E+OO' 0.00E+00 II.00E+OO 6.93E+0(1 6.93E+00 6.93E+0U 3.46E-03
_ o-Xvlcne HAP 9547-6 O.00E400 O.00E+00 O.00E-FOO 4.94E+00 4.94E+00 4.94E4(H) 2.47E-03
Ozone O.00E+OO 0.00E+00 0.00E+00 0.00E+00 O.00E+OO O.00E+00 0.00E+00
Pachloroethvlene(fetmchloroethene) 81 127-184 O.00E+00 0.00E+00 0.00E+00 2.69E-01 2.69E-01 2.69E-01 1.35E-04
Phenol 82 108-95-2 0.00E+00 000E+00 O.00E+00 5.33E+00 5.33E+00 5.33E+10 2.66E-03
Phos hine 71 O.00E+00 O.00E+00 - 11.00E+00 0.00E+00 O.00E+00 O.00E+00 O.UOE+00
Phosphorus - HAP 7723-14-0 0.00E+00 0.00E+00 0.00E+00 9.43E+01 9.43E+01 9.43E+01 4.71E-02
Selenium HAP SEC O.00E+00 0.00E+00 0.00E+00 2.21E+01 2.21E+0l 2.21E+01 1.11E-02
Stvrene 91 10042-5. U.00E+00 0.00E+00 O.00E+00 7.75E-01 7.75E-01 7.75E-01 3.88E-04 .
Toluene 97 108-88-3 O.O(1E+00 0.00E+00 O.00E+0O 2.06E+OI 2.06E+01 2.06E+01 1.03E-02.
Taal Fluorides(including H 50 - 1698448-8 0.00E+00 0.00E+00 O.DOE+00 5.87E+03 5.87E+13 5.87E+03 2.93E+00
Trichlom0uoromethane 100 75-694 O.UOE+00 .0.00E+00 0.00E+00 1.35E+00 135E+00 1.35E+00 6.73E-04
Vi7l acetate HAP 108-03-4 O.00E+00 0.00E+00 0.01E+00 9.62E-U3 9.62E-03 9.62E-03 4.81E-06
- vcue 104 1330-20-7 0.00E+00 O.00E+00 0.00E+00 1.5(IE+01 150E+01 1.50E+01 7.51E-03
Pinned:6/19=14 6upprnl 13f 3tiens File:El 1(113-Mo&k-S.x
- Page 13 d 36 - Sheet:Brkk-Sum

Title: 2013 Air Emission Inventory
Source ID#: ES-Coal-CC
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
Coal Crusher
Source: ES-Coal-CC Coal Crusher
Controls: CD-Coal-CC NA
Efficiency: 99.0%
Maximum Production: 4,261 tpy
r Uncontroll"ed x x ,� � .�
x Emtsston Factor "` Emisston`-
PollutantRate(lb/yr) T
N 4^ Y
PM 1.10 4.69E+01 2.34E-02
PM-10 1.10 4.69E+01 2.34E-02
PM-2.5 1.10 4.69E+01 2.34E-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)
I_
1.l lb/ton
Support Calculations File: El 2013-Moncure.xlsx
Printed:6/19/2014 Page 14 of 35 Sheet: ES-Coal Crusher

Title: 2013 Air Emission Inventory
Source ID#: ES-WFS
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
Wood Fuel/Sawdust System
G Source: ES-WFS Wood Fuel/Sawdust System
Hours of Operation 0 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-DC]
Source: ES-SD-SCI 8x8 Screen
ES-SD-SC2 8x8 Screen
i- ES-SD-CV1 Transfer Screw Conveyor
ES-SD-CV2 Screen Feed Screw Conveyor
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* I lb/7,000 gr*Flow Rate*60 min/hr
_ P1YI Emissions 01.80. . ; Ib/hr
0 lblyr
Printed:6/19/2014 Support Calculations File: El 2013-Moncure.xlsx
Page 15 of 35 Sheet: Controlled New WFS(G-21)

l �
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 cfm
Bagfilter Efficiency= 99%
Emissions Before Control
PM Emissions=Emissions After Control/(1 -Efficiency)
PM Emissions= 20.1 Ib/hr
Emissions After Control
PM Emissions=Exit Concentration* 1 lb/7,000 gr*Flow Rate*60 min/hr
pm Emrs§tons =0 201 !b/bi
Support Calculations File: El 2013-Moncure.xlsx
Printed:6/19/2014 Page 16 of 35 Sheet: Controlled New WFS(G21)

P
Wood Fuel/Sawdust System
Controls: CD-SD-BVl Bin Vent Filter
Description: Storage silo,which is connected to a bin vent filter,is used as storage for the product.
EPN: EP-SD-BV1
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/(I -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 Em�Ss>tons 0 0 '4 Ib/bIr
0 0 �.,� lb/yi•
Support Calculations File: El 2013-Moncure.xlsx
Printed:6/19/2014 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 Ib/7,000 gr*Flow Rate*60 min/hr
P1VI Em>sswns *4 0�'4 . ' 1blfir
Total WFS Emissions
wt
ota
-PolWtanh 4 (Controlled) TPY
PM 0.00E+00 0.00E+00
PM-10 0.00E+00 0.00E+00
PM-2.5 0.00E+00 0.00E+00
Support Calculations File: El 2013-Moncure.xlsx
Printed:6/19/2014 Page 18 of 35 Sheet: Controlled New WFS(G21)

Title: 2013 Air Emission Inventory
Source ID#: Clay Handling
Facility: - General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
Source: ES-CH Clay Handling Equipment
Description: This scenario represents the crushing/grinding/screening/storage operations as they
are currently operating.
EPN: Fugitive
Controls: NA
Factors for Grinding&Screening:
AP-42 Section 11.3,Table 11.3-2
Emission Factor for Grinding and Screening
PM emission factor 0.0250 lb/ton
PM-10 emission factor 0.0023 lb/ton
PM-2.5 emission factor 0.0023 lb/ton "
Maximum Process Throughput 200 tph
Actual Raw Material Processed 108,707 tpy
Maximum Hours of Operation 1,750 hrs/yr
Control Efficiency for PM 0 % No Control Devices
I .
77
Descr'ipdon
F-PC Primary crusher(clay handling
equipment 200 tph)
F-SS1 &F-SS2
handling equipment 200 tph)
F-HM Hammermill#1 (clay handling
equipment 200 tph)
F-FS1 -F-FS9
screens(clay handling equipment
F-FC4
handling equipment 200 tph)
F-FC5 Finishing Conveyor#5(clay
handling equipment 200 tph)
INSPS
Pollutanf= Acfual` m>tsstoixs
PMa (Ibsf' r 2,718 1.36
L PM-10 250 0.13
PM-2.5 250 0.13
Support Calculations File: El 2013-Moncure.xlsx
p Printed:6/19/2014 Page 19 of 35 Sheet: Clay Handling(G-71)

Title: 2013 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
i
Grinding&Screening Emissions
PM Actual Emissions(lbs/yr)
0.025 lb/ton * 108707.13 tpy = 2717.68 lbs/yr
PM Actual Emissions(tons/yr)
2717.67825 lbs/yr/2000lb/ton = 1.36 tpy
.PM-10 Actual Emissions(Ibs/hr)
0.0023 lb/ton* 108707.13 tpy = 250.026 Ibs/yr
PM-10 Actual Emissions(tons/yr)
250.026399 lbs/yr/2000lb/ton = 0.13 tpy
PM-2.5 Actual Emissions(Ibs/hr)
0.0023 lb/ton* 108707.13 tpy = 250.026 Ibs/yr
PM-2.5 Actual Emissions(tons/yr)
250.026399 Ibs/yr/2000lb/ton = 0.13 tpy
i
I-
Support Calculations File: EI 2013-Moncure.xlsx
Printed:6/19/2014 Page 20 of 35 Sheet: Clay Handling(G-71)

2013 Air Emission Inventory
General Shale Brick Inc.
Source: Intersite Conveyor Moncure Plant
Source: Conveyor from Cape Fear Plant to
Bri6khaven 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)^l.3/(M/2)^1.4](I-controleff/l00)lb/ton
where: E=emission factor(lb/ton)
k=particle size multiplier(dimensionless)
U=mean wind speed(mph)
M=material moisture content(%)
E=k(0.0032)[(U/5)^1.3/(M/2)^1.4]lb/ton
where:
k= 0.74 for PM<=30 microns;
0.35 for PM<=10 microns;
0.053 for PM<=2.5 microns;
U= 15 mph
- M= 10 % estimated from Table 13.2.4-1 of AP-42
PM<=30 microns:
0.74*0.0032*[(15 mph/5)^1.3/(10/2)^1.41= 1.04E-03 lb/ton.
PM<=10 microns:
0.35*0.0032*[(15 mph/5)^1.3/(10/2)^1.4]= 4.91E-04 lb/ton
PM<=2.5 microns:
0.053 *0.0032*[(15 mph/5)^1.3/(10/2)^1.4]= 7.43E-05 lb/ton
Basis: All emission sources for the proposed grinding room are listed below.
Control Efficiency for PM 0 % No Control Devices
The following source will be subject to NSPS.
Emissions estimated using the Drop Equations from AP42
Location ID Throughput brops
;: s I)escnphon
3 ;
^.t:
From Cape Fear to Brickh ES-C Conveyor M 108,707
aven 1
Pollutant Potential Emissions(per emission source)
PM
112.81 0.06
PM-10 53.36 0.03
PM-2.5 8.08 0.00
Emissions based on Drop Equations Equations @ 200 tph,which is the process weight rate for Brickhaven's
existing Grinding Room.
Printed:6/19/2 014 Support Calculations File: El 2013-Moncure.xlsx
Pa a 21 of 35
r 9 Sheet: IntersiteConv(Clay Handling)

SAMPLE CALCULATIONS
Grinding&Screening Emissions
PM Potential Emissions(lbs/yr)
0.001 lb/ton* 108707.13 tpy* 1 drop= 112.81 lbs/hr
PM Potential Emissions(tons/yr)
113 /20001b/ton = 0.06 tons/yr
TOTAL EMISSION CALCULATIONS FOR CLAY HANDLING
Poltant 1 We",
Potenf�al Em�srons{per em�ssron source)
_z IGs/ r ,
y) h. {tons/y'r)
PM 2830.49 1.42
PM10 303.38 0.15
PM2.5 258.11 0.13
I
Support Calculations. File: El 2013-Moncure.xisx
Printed:6/19/2014 Page 22 of 35 Sheet: IntersiteConv(Clay Handling)

r Title: 2013 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
Actual Brick Production-CIF 0 tons/yr
Actual Brick Production-BH 96,201 tons/yr
Hrs of Operation-Brick Haven 2000 hr/yr
Hrs of Operation-Cape Fear 0 hr/yr
Baghouse Efficiency 99.8%
Approach: AP42 Section 11.3,Table 11.3-2
I
AP-42 Emission Factor for PM/PM-I O/PM-2.5 0.0036 lbs/ton brick
j Basis: Actual Brick Production Rate-Cape Fear 0 tpy
Actual Brick Production Rate-Brickhaven 96201 tpy
Scale Up Factor Potentials 1
Two Texturing Operations
Controlled by CD-CR6BF, CD-CR7BF, CD-CR7BF2 and CD-CR7BF3
EMISSION CALCULATIONS
Brick Haven Brick haven Cape Fear Total
Pollutattt ual,Em�ss><gns � Actual Em>tssons,,, `.Actual Emiss>lons";
r)
PM 346.32 0.173 0.00 0.000 346.32 0.173
PM-10 346.32 0.173 0.00 0.000 346.32 0.173
PM-2.5 346.32 1 0.173 0.00 0.000 346.32 0.173
i
Support Calculations File: El 2013-Moncure.xlsx
Printed:6/19/2014 Page 23 of 35 Sheet: Text(G-69)

Title: 2013 Air Emission Inventory
Source ID#: ES-CD-8
Description: Rotary Coatings Dryer
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
Source: ES-CD-8 Rotary Coatings Dryer
Description: Sand is dried in the rotary coatings dryer -
EPN: EP-CD-8
Controls: CD-CDBBF
Variables: Hours of Operation
Dryer Fuel: Natural Gas with Propane/Air Standby
i
Dryer Gas Rate(MMBtu/hr)= 0.25 MMBtu/hr
Hours of Operation= 300 hrs
Bagfilter Control Efficiency= 99.9%
Heating Value for Natural Gas= 1020 Btu/ft3
2011 Gas Usage(Calculated 7.35E-02 mmft3/yr -
based upon hours of operation)_
Unc4 ns Emrssrons
Pollutant^ (Ib/mmft3) .x Re£ 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 ' 4.41E-02 2.21 E-05
NOx 100 ' ' 7.35E+00 3.68E-03
VOCs 5.5 ' 4.04E-01 2.02E-04
CO 84 ' 6.18E+00 3.09E-03
2-Methylnaphthalene 2.40E-05 ' 1.76E-06 8.82E-10
3-Methylchloranthrene 1.80E-06 ' .1.32E-07 6.62E-11
7,12-Dimethylbenz(a)anathracene 1.60E-05 ' 1.18E-06 5.88E-10
Acenaphthene 1.80E-06 '. 1.32E-07 6.62E-11
Acenaphtylene 1.80E-06 ' 1.32E-07 6.62E-I1 -
Anthracene 2.40E-06 ' 1.76E-07 8.82E-II
Benz(a)anthracene 1.80E-06 ' 1.32E-07 6.62E-II
Benzene 2.10E-03 ' 1.54E-04 7.72E-08
Benzo(a)pyrene 1.20E-06 ' 8.82E-08 4.41E-II
Benzo(b)fluorarithene 1.80E-06 ' 1.32E-07 6.62E-II -
Support Calculations File: El 2013-Moncure.xlsx
Printed:6/19/2014 Page 24 of 35 Sheet Dryer(ES-CD-8)

Benzo(g,h,I)perylene 1.20E-06 1 8.82E-08 4.41E-II
Benzo(k)fluoranthene 1.80E-06 1.32E-07 6.62E-II
Butane 2.1 1.54E-01 7.72E-05
Chrysene 1.80E-06 I 1.32E-07 6.62E-II
Dibenzo(a,h)anthracene 1.20E-06 I 8.82E-08 4.41E-II
Dichlorobenzene 1.20E-03 I 8.82E-05 4.41E-08
Ethane 3.1 1 2.28E-01 1.14E-04
Fluoranthene 3:00E-06 1 2.21 E-07 1.10E-10
Fluorene 2.80E-06 I 2.06E-07 1.03E-10
Formaldehyde 7.50E-02 1 5.51E-03 2.76E-06
Hexane 1.8 1 1.32E-01 6.62E-05
Indeno(1,2,3-cd)pyrene 1.80E-06 I 1.32E-07 6.62E-II
Naphthalene 6.10E-04 ' 4.49E-05 2.24E-08
Pentane 2.6 1 1.91E-01 9.56E-05
Phenanathrene 1.70E-05 I 1.25E-06 6.25E-10
Propane 1.6 ' 1.18E-01 5.88E-05
Pyrene 5.00E-06 I 3.68E-07 1.84E-10
Toluene 3.40E-03 1 2.50E-04 1.25E-07
Arsenic 0.00E+00 2 0.00E+00 0.00E+00
Barium 4.40E-03 I 3.24E-04 1.62E-07
Beryllium 0.00E+00 2 0.00E+00 0.00E+00
Cadmium 0.00E+00 2 0.00E+00 0.00E+00
Chromium(as chromic acid) 0.00E+00 2 0.00E+00 0.00E+00
Cobalt 8.40E-05 I 6.18E-06 3.09E-09
Copper 8.50E-04 I 6.25E-05 3.13E-08
CO2 1.20E+05 2 8.82E+03 4.41E+00
Lead 5.00E-04 I 3.68E-05 1.84E-08
Manganese 0.00E+00 2 0.00E+00 0.00E+00
Mercury 0.00E+00 2 0.00E+00 0.00E+00
Methane 2.30E+00 I 1.69E-01 8.46E-05
Molybdenum 1.10E-03 I 8.09E-05 4.04E-08
N20 2.20E+00 I 1.62E-01 8.09E-05
Nickel 0.00E+00 2 0.00E+00 0.00E+00
Selenium 2.40E-05 I 1.76E-06 8.82E-10
Vanadium 2.30E-03 I 1.69E-04 8.46E-08
Zinc 2.90E-02 ' 2.13E-03 1.07E-06
' AP-42;Compilation of Air Pollutant Emission Factors Vol. 1 Stationary Sources USEPA,
5th ed.Section 1.4,3/98-Small Boilers-Uncontrolled
z NC Department of Air Quality,Natural Gas Spreadsheets-Small Boiler-Uncontrolled
3 PM&PM-10 Emissions were calculated by adding natural gas combustion factors and(AP-42,Section
1.4)and factors for industrial sand dryers(AP42,Section 11.19)
Support Calculations File: El 2013-Moncure.xlsx
Printed:6/19/2014 Page 25 of 35 Sheet: Dryer(ES-CD-8)

i
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*2 lb/ton
PM/PM-10/PM-2.5 Emissions= 6.90 lb/hr
PM/PM-10/PM-2.5 Emissions= 30222 ton/yr*2 lb/ton
PM/PM-10/PM-2.5 Emissions= 60,444 lb/yr
Controlled Emissions= 60 lb/yr
* Due to the lack of emission factors for this type of operation,the industrial sand
dryer emission factor from AP42,Section 11.19 was selected for use. It is felt that _
this is a conservative factor because the factor is for mined quartzite that is
processed into sand,which is normally a dirtier operation than is conducted for
coatings at brick plants.
i
Support Calculations File: El 2013-Moncure.xlsx
Printed:6/19/2014 Page 26 of 35 Sheet: Dryer(ES-CD-8)

Title: 2013 Air Emission Inventory
Source ID#:ES-VS1,-VS2,-VS3,-VS4,&-VS5
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID h 1900009
Vacuum Systems
The vacuum systems,which all connect to a bag filter,are used to collect particulate matter from the empty kiln cars
at both the Brickhaven and Cape Fear Plants. VS-3 is used to remove sand at the sand seal discharge at the
Brickhaven Plant.
FACTORS Exit Concentration= 0.01 gr/dscf
Flow Rate for System= 1400 cfm
Bagfilter Efficiency= 99.9%
G-70 Hours of Operation-Cape Fear= - hr/yr
(IES-V S 1)
Hours of Operation-Brick Haven= - hr/yr
(IES-VS2)
Total - hr/yr
G-22 Hours of Operation-Brick Haven= 2,000 hr/yr
(IES-VS3)-Kiln 3 Hi-Vac
Hours of Operation-Brick Haven= - hr/yr
(IES-VS4&-VS5)
Total 2,000 hr/yr
Emissions Before Control
PM Emissions=Emissions After Control/(1 -Efficiency)
PM Emissions= 120.0 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
PM-2.5 Emissions= 0.120 lb/hr
EMISSION CALCULATIONS
Actual Emissions=PM Emissions,lb/hr(After Control)*Hours of Operation,hr/yr
G-70(IES-VS1 &-VS2)
Pollutant <.' v,, ' A' ual.Emissions BH',., Actual Emissions GF ,, Total;Actual Emissions3
Name Ibs% r tons/ r (IbS/yr) ,, (tons%yr) (lbsY (tbnslyr)
PM 0.00 0.000 0.00 0.000 .0.00 0.000
PM-10 0.00 0.000 0.00 0.000 0.00 0.000
PM-2.5 0.00 0.000 0.00 0.000 0.00 0.000
G-22(IES-VS3,-VS4&-VS5)
Pollutant ;ActualEmissions-VS3' - Actual-Emissions VS4:&VS$ otal Actual Emissions
Name .. Ib"s/ r . tons/ r..'.' (Ibs%yr) (tons%yr),,.,, r ,(Ibs/yr) ;(tons/yr)
PM 240.00 -0.120 0.00 0.000 240.00 0.120
PM-10 240.00 0.120 0.00 0.000 240.00 0.120
PM-2.5 240.00 0.120 0.00 0.000 240.00 0.120
Support Calculations File: El 2013-Moncure.xisx
Printed:6/19/2014 Page 27 of 35 Sheet: Vacuums(G-22&G-70)

Title: 2013 Air Emission Inventory
Source ID#: Storage Tanks
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID M 1900009
Turnoversyank
11
9"
k
b 11 Description/,Conteqts-,5q,,, Size
Diesel 1,000 7 5 881 27,915 31.68 0.14 0.88 1.02
Gasoline 1,000 7 5 1,028 2,743 2.67 163.34 26.31 189.65
Waste Oil 275 5.25 3 225 500 2.22 0.00 0.00 0.00
Motor Oil 160 4.5 2.5 129 165 1.28 10.86 0.64 11.50
Brick Oil 350 6.5 3 291 3,000 10.32 15.60 10.74 26.34
Gear Oil 350 6.55 3 346 600 1.73 15.60 1.67 17.27
39,923 Total(lb/yr)= - 245.78
Total(ton/yr)= 0.123
Support Calculations. File: El 2013-Moncure.xlsx
Printed:6/19/2014 Page 28 of 35 Sheet: Storage Tanks(G-W)

Title: 2013 Air Emission Inventory
Source ID 6: ES-BP-FAS
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID 9:1900009
So
urceEmissmn
"Devicc'ID,
Fi
PM Era PM o EM
t escnp low
Flyash Sil, 3-05-011-06 bin vent 0.0099 0.0049 0.0049 0 0.00E+00 0.001;�M0 0.00E+00 0.00E+00 0.0013+00 0.00E+00
a Controlled PM emission factors for aggregate transfer,pneumatic flyash loading,pneumatic loading of'cement silo,weigh hopper loading,and mNer loading from AP42,Section 11.12-
Concrete Batch Operations,(10/01).
yash"
-SHOMIRW
Eltials'shm ash Sit
Hai�ardous Air 'Factor,.-
Example Calculations:
:';.,
Pollutant (I V1(6 u
Arsenic 1.00E-06 0.0011+00 0.00E+00 PM Potential Emissions(lbs/yr)
Beryllium 9.04E-08 0.0013+00 0.00E+00 0.0091b/ton*Otpy=lbsAT 0 lbs/w
Cadmium 1.9813-08 0.0011+00 0.0013+00
Chromiun 1.22E-06 0.0013+00 0.0013+00 PM Potential Emissions(tonslyr)
Lead 5.20E-07 0.00E+00 0.0013+00 0 lbs/y,,•(I ton/2000 lb)= 0.00E+00 tons/)T
Manganes 2.56E-07 O.00E+00 0.00E+00
Nickel 2.2813-06 0.0011+00 0.0013+00
Phospho 3.5413-06 0.0011+00 0.0013+00
Selenium 7.24E-08 0.0011+00 0.00E+00
Support Calculatio File:E12013-M.-id.
Printed:611912014 Page 29of35 Sheet Ftyash Silo

Title: 2013 Air Emission Inventory
Source ID ES-BP-CS
Facility: General Shale Brick Inc.
Location: Moncure,NC
Facility ID 0:1900009
-"!Pofito
_PW,
Emissiow JID' E V hr,6
i2n
tpy)",-'*, t bftob),z':
Cement S 3-05-011-07 bin vent 0.00099 0.00034 0.00034 0_ 0.0013+00 0.0011+00 0.00E+00 0.00E+00 0.00E+00 0.0013+00
a Controlled PM mission factors for aggregate transfer,pneumatic flyash loading,pneumatic loading of cement silo,%nigh hopper loading,and mixer loading from AP-12,Section
11.12-Concrete Batch Operations,(10/0 1).
Ce'm e'n't S I 10,
Hazardous, -,4 Emission '.Cement Silo Emissions;."
Factors r. Example Calculations
lutant. ..On -(lbly)
Arsenic 4.24E-09 0.0013+00 0.00E+00 PM Potential Emissions(lbstyr)
Beryllium 4.8613-10 0.00E+00 0.00E+00 0.00999lb/ton*Olpy=lbs/)T 0 lbsfyr
Cadmium 4.8611-10 0.00E+00 0.00E+00
Chromiun 2.90E-07 0.0013+00 0.00E+00 PM Potential Emissions(tonstyr)
Lead 1.0913-08 0.0011+00 0.00E+00 0 lbstyr•(I ton/2000 lb)- 0.0013+00 tons/yr
Mangan s 1.1713-07 0.00E+00 0.00E+00
Nickel 4.1 8E-05 0.0011+00 0.00E+00
Phosphon
Selenium
Support Calculations File:El 2013-Monweift
Printed:6119/2014 Page 30 of 35 Sheet:Cement Sdo

Title: 2013 Air Emission Inventory
Source ID 9: ES-BP-BM
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility EDO: 1900009
Controlled 'Controlled
"T aSmurce-,1
Classfieadon ;sion Etnrssron
;-, codi(SCC) Denee Fac
tor
FaMor FactorThraugEiisium.Soure e h
``;Uc&cnptlonv; 0 tcm",�'
Mixer Loading 3-05-011-09 bagfifter 0.011 0.0038 0.0038 0 0.00E+00 O.00E+OL 0a00E+00 i`�0.1-0012+00 0.0011+00 0.00E+00
a Controlled PM emission factors for aggregate transfer,pneumatic flyash loading,pneumatic loading ofmmct silo,weigh hopper loading,and mixer loading from AP42,Section 11.12-
Concrete Batch Operations,(10/0 1).
''Batch
I er,
...,E, s io-
Ha'iardous Am' Example Calculations:
Arsenic 1.87E-08 0.0000 0.00E+00 PM Potential Emissions(lbs/vr)
Beryllium 0.011 lb/ton*Otpy-lbs6T 0 lbs/i
Cadmium 7.10E-10 0.0000 0.00E+00
Chromium 1.27E-07 0.0000 0.0013+00 PM Potential Emissions(torr/vr)
Lead 3.66E-08 0.0000 0.0013+00 0 lbsAT•(I ion/2000 lb) 0.00E+00 tcna�%r
Manganese 3.78E-06 0.0000 O.00E+00
Nickel 2.48E-07 0.0000 0.00E+00
Phosphorus 1.20E-06 0.0000 0.00E+00
Selenium
Printed:611g2014 Support Calculations File.El 2013-Monevre.xfsx
Page 31 of 35 Sheet Batch Mixer

EMISSION CALCULATIONS General Shale Brick
Source: ES-RUMBLE Rumbler
Description: Rumbler tumbles blocks in a rotating drum in order to create an "aged" look.
EPN: EP-RUMBLE
Controls: Baghouse CD-RUMBLE
Hours of Operation: 0 hrs
Factors:
Exit Concentration= 0.01 gr/dscf
Flow Rate for System= 5000 cfm .
Bagfilter Efficiency= 95%
Emissions Before Control
PM/PM-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 Cadtrolled.Actual.Fm>Iss><ons
Name z ; & (Ibs/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
Support Calculations File: El 2013-Moncure.xlsx
Printed:6/19/2014 Page 32 of 35 Sheet: Rumbler

420'b5 :CJ� 1 '/8 ; 2
05
ON d
� c."�� c uai f.z�/n�j v� ��og.� � � movie S o l•�r�ua x �4��r�••.�o
7�%9/ '/ 70-srog'z CI>A
�99* '/Z L '9'06 `Z�- x(2ry
fi Z9 •L!s 8 •%o 'S f, -z os
---
wy
_
S'Z90 Z -� 8 •emu ' oF3'v �� s-s'/! �/9 L
e'�ao8 'z zs•�zt� �•z o•o P, 'S8£'/ lyZo•o OA 5-0 7/ /
L'9Gb'Z!�'' Sib-'Z♦ S�'� L ',Z��'(� /ter•p xp�y £-£ '/J 9'�'l
BL �Sz L%"Q Z '9127, 'b% Z / CS -�•// �.
t�o•-,>JI"a'Oro/ bL 8•L too
'�o/
C���, lr�stnr� �•3 .1Nbt�J �'''
s3�.�j�� d o �dr'►� so►S��►x�v1v �c� �on�Qr ?�o�
CoBb"SE)
- ,. , %g�'b/ •� vx�a �N � 'dam _ 'J%Y CXob
I Z-so i oz b ooOpb/

2 � f
°sf
Title: 2013 Air Emission Inventory
Source ID#: ES-K4K
Facility: General Shale Brick,Inc.
Location: Moncure,NC
Facility ID#: 1900009
Brick Processing System-Brick Haven-Kiln 4
Source: ES-K4K Kiln 4
Actual Brick Production: 96,201 Tons/yr
Coal Fired 4,261 Tons/yr
Brick Kiln Fuel: CoaVNG
60%Coal
40% Natural Gas
Control Eff.of HF 90% (NESHAP Requirement)
Uncontrolled
Uncontrolled Emission
TAP NO. Emission Ref Factor for Tested Total
Factor for Coal Natural Gas Emission Annual Annual
Pollutant from AP42 from AP-42 Ref Factors Ref Emissions Emissions
(lb/ton) (lb/ton) (lb/ton) (lb/ r) (ton/ r)
PM 4.12E-01 9 96376.88 4.82E+01
PM-10 2.03E-01 9 76242.99 3.81E+01
PM-2.5 2.03E-01 9 76242.99 3.81E+01
SO2 AM38.000 f 2.86E-02 d 163018.56 8.15E+01
NOx 8.13E-01 78239.16 3.91E+01
VOC 2.40E-02 A 2.40E-02 ad 2308.82 1.15E+00
CO 8.00E-01 ab 0.83 ai 78115.21 3.91E+01
Chlorine 29 1.30E-03 of 125.06 6.25E-02
HF 59 3.81E-01 d 3668.48 1.83E+00
HCl 57 5.82E-02 d 5599.255 2.80E+00
III-Trichloroethane 68 1.70E-05 4.70E-06 of 1.16E+00 5.81E-04
(methylchloroform)
Methylene Chloride 69 8.00E-07 ae 7.70E-02 3.85E-05
Perchloroethylene 81 2.80E-06 of 2.69E-01 1.35E-04
(Tetrachloroethene)
1,1-dichloroethane HAP 5.00E-06 ec 4.81E-01 2.41E-04
1,4-dichlorobenzene 36 3.20E-06 ee 4.80E-05 of 2.03E+00 1.02E-03
2-butanone(MEK) 70 2.50E-04 a` 2.20E-04 of 2.29E+01 1.14E-02
2-Hexanone NA 9.40E-07 a` 8.50E-05 ar 3.33E+00 1.66E-03
2-methylphenol(cresol) 35 2.20E-06 a` 2.12E-01 1.06E-04
2-methylnaphthalene NA 1.70E-06 ac 5.70E-05 of 2.29E+00 1.15E-03
Antimony NA 2.70E-05 ah 2.60E+00 1.30E-03
Acetone NA 6.80E-04 ac 1.70E-03 of 1.05E+02 5.23E-02
Arsenic 9 1.30E-04 ag 3.10E-05 ah 8.70E+00 4.35E-03
Benzene 12 2.90E-04 a` 2.90E-03 ac 1.28E+02 6.42E-02
Benzoic Acid 2.50E-04 a` 2.41 E+01 1.20E-02
Beryllium 16 1.60E-05 ag 4.20E-07 ah 9.40E-01 4.70E-04
Bis(2-ethylhexyl)phthalate; 2.00E-03 of 8.12E+01 4.06E-02
di(2-ethylhexyl)phthalate 39 7.30E-05
Bromomethane(Methyl HAP 2.40E-05 2.31E+00 1.15E-03
Bromide)
Support Calculations File: El 2013-Moncure.xlsx
Printed:6/19/2014 Page 9 of 35 Sheet: Brick-BH(ES-K4K_G12)NG&Coal

Butylbenzylphthalate NA 1.20E-06 " 1.80E-05 of 7.62E-01 3.81 E-04
Cadmium 23 1.50E-05 ah 1.44E+00 7.22E-04
Carbon Disulfide 27 2.30E-06 w 4.30E-05 of 1.79E+00 8.94E-04
Carbon tetrachloride 28 1.00E-07 9.62E-03 4.81E-06
Chlorobenzene HAP 2.10E-05 2.02E+00 1.01E-03
Chloroethane(Ethyl HAP 1.10E-05 w 5.70E-04 of 2.26E+01 1.13E-02
Chloride)
Chloroform 31 1.00E-07 '° 9.62E-03 4.81 E-06
Chloromethane(Methyl HAP 1.10E-04 w 6.70E-04 I 3.21E+01 1.61E-02
Chloride)
Soluble Chromate 5.10E-05 'h 4.91E+00 2.45E-03
Compounds
Cobalt 2.10E-06 ah 2.02E-01 LOIE-04
Dibenzof rran NA 3.60E-07 " 3.46E-02 1.73E-05
Diethylphthalate HAP 1.40E-06 - 2.40E-04 of 9.32E+00 4.66E-03
Dimethylphthalate HAP 7.80E-07 7.50E-02 3.75E-05
Di-n-butylphthalate HAP 1.40E-04 at 1.35E+0I 6.73E-03
Di-n-octylphthalate 1.20E-05 1.15E+00 5.77E-04
Ethylbenzene HAP 2.10E-05 4.40E-05 If 2.91E+00 1.45E-03
Formaldehyde 51 7.50E-02 b - 9.52E-07
lodomethane(Methyl HAP 9.30E-05 'r 8.95E+00 4.47E-03
Iodide)
lsophorone HAP 3.00E-05 2.89E+00 1.44E-03
Lead NA 1.50E-04 ah 1.44E+01 7.22E-03
M-/p-Xylene HAP 1.30E-04 6.70E-05 ar 1.01E+01 5.04E-03
Manganese 62 2.90E-04 as 2.90E-04 ah 2.79E+0l 1.39E-02
Mercury 66 9.60E-05 at 7.50E-06 ah 5.83E+00 2.91E-03
Naphthalene HAP 6.90E-06 '< 6.50E-05 - 2.90E+00 1.45E-03
Nickel 75 7.20E-05 ah 6.93E+00 3.46E-03
o-Xylene HAP 4.70E-05 5.80E-05 - 4.94E+00 2.47E-03
Perchloroethylene of 2.69E-01 1.35E-04
(Tetrachloroethene) 81 2.80E-06
Phenol 82 3.50E-05 ' 8.60E-05 as 5.33E+00 2.66E-03
Phosphorus HAP 9.80E-04 ag 9.43E+01 4.71E-02
Selenium NA 2.30E-04 ah 2.21E+O1 I.11E-02
Styrene 91 1.00E-07 11 2.00E-05 ae 7.75E-01 3.88E-04
Toluene 97 2.50E-04 - 1.60E-04 - 2.06E+01 1.03E-02
Total Fluorides 50 6.10E-01 c 5.87E+03 2.93E+00
Trichlorofluoromethane 100 1.40E-05 - 1.35E+00 6.73E-04
Vinyl acetate HAP 1.00E-07 - 9.62E-03 4.81E-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 /
abTable 11.3-3 for coal-fired and natural gas-fired kilns..F = 7,`E�Z
"Table 11.3-4 for coal-fired and natural gas-fired kilns
ad Table 11.3-5 for brick kilns. v
'Table 11.3-6 for coal-fired kilns. J c.,l5~�Z-�74.6
at Table 11.3-6 for natural gas-fired kilns t�/.'-7 U L :3 ca-n
'gTable I I3-7 for coal-fired kilns.
'n Table 11.3-7 for natural gas-fired kilns.
a'Factor is from AP-42 Background Document testing at
Marseilles Brick which has the same type of kiln
of Soluble Chromate Compounds is the regulated NC TAP
h Emission factors from AP-42,Section 1.4,7/98. The emissions factor in in Ib/mmft'of gas. The actual gas rate:
Formaldehyde Emission Factor=
25.9 MMBtu/hr/1020 Btu/ft1•I e Btu/MMBtu/I O^(f 0.0254 mmftl/hr
Support calculations File: El 2013-Moncure xlsx
Printed:6119=14 Page 10 of 35 Sheet: Brick-BH(ES-K4K_G 12)NG&Coal

I�
I
h Title: 2013 Air Emi
Source ID M Summary .
Facility: General Shal
Location: Moncure,N(
Emissions Summary
St6rg Total otal
Bollutant Cas-Numb(ixer -Rumbler Tanks (lblyr) (TPY)
PM 00 0.00E+00 1.18E+05 58.95
PM-10 00 O.00E+00 9.52E+04 47.61
PM 2.5 00. 0.00E+00 9.52E+04 47.59
SO2 1.63E+05 81.51
_ NOx 8.77E+04 43.84
VOC 1.23E-01 5.44E+03 2.72
CO 1.05E+05 52.53
1
1,4-dichlorobenzene 106-46-7) 2.03E+00 1.02E-03
2-butanone(MEK) 78-93-3 1 2.29E+01 1.14E-02
2-methylphenol(cresol) 9548-7 f 2.12E-01 1.06E-04
Acrylonitrile 107-13-1r 0.00E+00 0.00E+00
Antimony kNTIMONYO,. 2.60E+00 130E-03
Arsenic ARSENICCgoo 8.70E+00 4.35E-03
Benzene 7143-2 1 1.28E+02 6.42E-02
Benzo(a)pyrene, 30-32-8 1 8.82E-08 4.41E-11
Beryllium BERYLCPI 9.40E-01 4.70E-04
Bis(2-ethylhexyl)phthalate;di(2-
eth lhex 1)phthalate 117-87-71 8.12E+01 4.06E-02
Bromomethane(Methyl Bromide) 74-83-9 1 2.31E+00 1.15E-03
Cadmium CADMIUMC 00 1.44E+00 7.22E-04
Carbon Disulfide 75-15-0 1.79E+00 8.94E-04
Carbon tetrachloride 56-23-5 9.62E-03 4.81E-06
Chlorine 7782-50-5 1.25E+02 0.06
Chloroethane(Ethyl Choroethane) 75-00-3 1 2.26E+01 1.13E-02
Chloroform 67-66-3 9.62E-03 4.81 E-06
Chloromethane(Methly Chloride) 74-87-3 3.21E+01 1.61E-02
Chromium CROMCPD00 4.91E+00 2.45E-03
Cobalt ff7440-48-44 2.02E-01 1.01 E-04
Diethylphthalate - 9.32E+00 4.66E-03
Dimethylphthalate 7.50E-02 3.75E-05
Di-n-butylphthalate 1.35E+01 6.73E-03
File: El2013-Moncure.xlsx
Printed:6/19/2014 Sheet: Summary

,I
i
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
r piles
6. Coal hopper and coal pile
j
I
6/19/2014,FUG-BI-Monc.doc Page 35 of 35

APPENDIX A
TANKS 4.09 CALCULATIONS
General Shale Brick, Inc. -Moncure, NC Facility I CY 2013 Emissions Inventory
Trinity Consultants

I
TANKS 4.0 Report Page 1 of 6
TANKS 4.0.9d
Emissions Report-Detail Format
Tank Indentification and Physical Characteristics
Identification
User Identification: Moncure-Brick oil(350 gallons)
_ City: Moncure
State: North Carolina
Company. General Shale Brick
Type of Tank: Vertical Fixed Roof Tank
— Description: El-Brick oil tank(350 gallons)
_ Tank Dimensions -
Shell Height(ft): 7.50
Diameter(ft): 3.00
Uquid Height(ft): 6.50
Avg.liquid Height(ft): 6.50
Volume(gallons): 343.70
Turnovers-. 10.32
- Net Throughput(gai/yr): 3,546.98
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) 0.00
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 '
V
file:///C:/Pro9ram%20Files/Tanks4O9d/summarydisplay.btm 6/12/2014

TANKS 4.0 Report Page 2 of 6
TANKS 4.0.9d
Emissions Report-Detail Format
Liquid Contents of Storage Tank
Moncure-Brick oil(350 gallons)-Vertical Fixed Roof Tank
Moncure,North Carolina
Liquid
Daily Liquid 5url. Built Vapor liquid Vapor
Temperahpe(deg F) Temp Vapor Pressure(>sia) Mol. Mass Mass M.I. Basis for Vapor pressure
MixWreCCerop—t Manth Avg. Min. Maa. (deg F) Avg. Mn. Max. Weight Fr Frau Weight Ca1Wallona
Crude od(RVP 5) AO 68.49 57.95 79.03 62.36 3.3910 Z7639 4.1Z72 50,0000 -_- 207.00 Option 4:RVP=S -_
i
file:///C:/Program%2OFiles/Tanks4O9d/stimmarydisplay.htm 6/12/2014

TANKS 4.0 Report Page 3 of 6
,. TANKS 4.0.9d
Emissions Report-Detail Format
Detail Calculations(AP-42)
r
Moncure-Brick oil(350 gallons)-Vertical Fixed Roof Tank
Moncure,North Carolina
' Anrrual Errisson GkaWatigls
Standing Losses(lb): 15.6006 -
vapor Spam volume(ar ft): 8.9012 -
Vapor Density(Wear ftr 0.0299
Vapor Spam Expansion Factor. 0.1968
Vented Vapor S,h Ix n Factor, 0.8155
Tank Vapor Spam Volume:
Vapor Spam Voiure(cu ft): 8.9012 -
'I Tank Dia-fer(ftl: 3.0000
Vapor Spam Ouage(it)- 1,2593
Tank Shell Height ft 7.60M
Average Liquid Height(ft): 55000 _
Real Outage(it): 02593
Roof Outage(Dome RmQ
Roof Outage(it): 0.2593
Dome Radius(ft): 0,0000
Shell Radius(it): 1,5000
Vapor Deruty
Vapor Density([him ftF 0.0299
Vapor Molecular Weight(Ibnbmole): 50,0000
Vapor Pressure at Daily Average Liquid
Sunlam TemperaWra(p ia): 3.3910
Daily Avg.Liquid Sufam Temp.(deg.It): 528.1618
Daily Average Ambient Temp,(deg,F): 69.2833
Ideal Gas Constant R
(psia raft!(Qmol-deg R)y 10.731
Liquid Bulk Temporal u r(deg.R): 522.0333
Tank Paint Solar Absorptanm(Shell): 0,6800
Tank Pant Solar Absorpta=(R-Q: 0.6800
Daily Total Solar Inadation
Factor(Btdsgft day): 1.393.0797
Vapor Spam Expansion Fader
Vapor Spam Expansion Factor: 0.1988
Daily Vapor Irrperehge Range(deg.R): 42.1602
Daily Vapor Pressure Range(play 1.3633
Breather Vent Press,Setting Ra nge(psia): 0.0600
Vapor Pressure at Daily Average Liquid
Sudan Temperature(pia): 3.3910
Vapor Pressure at Da0y Mirxmum Liquid
Sudan Temperature(Pia): 2.7639
Vapor Pressure at Daly Maximm id u Liqu
Sufam Temperature(pia): 4,1272
Daily Avg.Liquid Surface Temp.(deg R): 528,1618
Daily Mn,Liquid Surface Temp.(deg R): 517.6217
Daily Max.Liquid Surface Temp.(deg R): 638.7018
Daily Ambient Temp.Range(deg.R): 21.7167
Vended Vapor SaWretion Factor
Vented Vapor Sahgation Fedor, 0.8155 _
Vapor Pressure at Daily Average Liquid:
Su=TempereWm(pia): 3.3910
Vapor Spam Outage(it). 1.2593
Working Losses(to): 10.7390
Vapor Molecular Weight 0bltomde): 5O.0000
Vapor Presage at Daily Av ge Liquid
Surlam Temperature(psi.): 33910
Amoral Net Throughput(gavyr.): 3,5a8.9792
A.-;Tom- 10.3200
Tumovar Fedor: 1.0000
Marimun Liquid Volume(gal): 343.6995
Mar-Ugidd Heigh,(ft): 6.5000
Tank Diameter(8): 3,0000
1 Witerg Loss Product F.=,. 07500
Toal Losses([by. N.3397
I
file:///C:/Program%2OFiles/Tanks4O9d/Summarydisplay.htm 6/12/2014

TANKS 4.0 Report Page 5 of 6
TANKS 4.0.9d
Emissions Report-Detail Format
- Individual Tank Emission Totals
Emissions Report for:Annual
Moncure-Brick oil(350 gallons)-Vertical Fixed Roof Tank
Moncure,North Carolina
Losses(lbs)
Components Working Loss Breathing Loss Total Emissions
Crude oil(RVP 5) I0.7J41 15.601126.34
l
i
file:///C:/Program%2OFiles/Tanks4O9d/summarydisplay.htm 6/12/2014

TANKS 4.0 Report Page 1 of 6
TANKS 4.0.9d
Emissions Report-Detail Format
Tank Indentification and Physical Characteristics
- - Identification
User Identification: Moncure-Diesel(1000 gallon)
City: Moncure
- state., North Carolina
Company: General Shale Bride
Type of Tank: Vertical Rxed Roof Tank -
Description: El-1000 gallon diesel tank-Moncure
Tank Dimensions
Shell Height(ft): 8.00
Diameter(ft): - 5.00
Liquid Height(ft): 7.00
Avg.Liquid Height(ft): 7.00
Volume(gallons): 1,028.16
Turnovers-. 31.68
Net Throughput(gal/yr): 32,572-14
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
Meterotogical Data used in Emissions Calculations:Raleigh,North Carolina(Avg Atmospheric Pressure=14.53 psia)
file:///C:/Program%2OFiles/Tanks4O9d/summarydisplay.htm 6/12/2014

TANKS 4.0 Report Page 2 of 6
TANKS 4.0.9d
Emissions Report-Detail Format
Liquid Contents of Storage Tank
Moncure-Diesel(1000 gallon)-Vertical Fixed Roof Tank
Moncure,North Carolina
Wed
Dady Upid Std. Bulk Vapor L'ged V.P.
T—pentue(deg F) Temp V.P.Pressure(Psi.) M.I. Mass Mass M.I. Bass for Vapor Pressue
Muture/Co pnnent MaMh Avg. Min. Max, (deg F) Avg. Min. Max. Weight. Fraa Frea Weight Caleulatioro
.___ _. ____...... _.__.._____.___— _
DMOam hnl or ro.2 AO 68.49 57.95 79.03 6236 0.0088 0.0069 0.0117 130.0000 189.00 Option 1:VP60=.0074 VP70 .009
- l
I
file:///C:/Program%2OFiles/Tanks4O9d/summarydisplay.htm 6/12/2014

TANKS 4.0 Report Page 3 of 6
TANKS 4.0.9d
Emissions Report-Detail Format
Detail Calculations(AP-42)
Moncure-Diesel(1000 gallon)-Vertical Fixed Roof Tank
Moncure,North Carolina
Annual Emission Caksulations
Standing Losses(lb): 0.1371
Vapor Space Volume(m ft): 24.6091
Vapor Density(INa ft): 0.0002
Vapor Spans Expansion Factor. 0.0760
Vended Vapor Saturation Factor 0.9994
Tank Vapor Spars Volume:
Vapor Spam Volume(m ft): 24.6091
Tank D'ameter(ft): 5.0000 -
VaporSpam Outage(ft): 125M
Tank Shell Haft(fty. 8.0000
Average Liquid Height(ft): 7.0000
Roof Outage(fty 02533
Roof Outage(Dome Root) _
Roof Outage(ft): 0.2533
Dome Radius(it): 5.0000
Shell Radius(ft): 2.5000 -
Vapor Density
Vapor Density(Ibfcu ft): 0.0002
Vapor Molecular Weight(fb/mvnole): 130.0000
Vapor Pre.sure at Daily Average Liquid
Surface Temperature(psi,): 0.0088
Daily Avg.Liquid Surface Temp.(deg.R): 528.1618
Daily Aveage Ambient Temp.(deg.F): 59,2833
Ideal Gas CorsWnt R
(psi.raft t(mTemperatureg R)): - 10.731
Liquid Bulk Temperature(deg.R): 522.0333
Tank Paint Solar Absorptance(Shell): O.68t10' -
Tank Paint Solar Absorptance(RmQ: 0.68W
Daily Total Solar Insulaten
Fader(BtWsgft day): 1.393.0797
Vapor Spam Expansion Factor
Vapor Spam Expansion Factor. 0.0760 -
Daily Vapor Temperature Range(deg.R): 42.1602
Daily Vapor pressure,Range(psi,): 0.0049
Breather Vent Press.Setting Ranga(psia): DOWD
Vapor Pr-ure at Daily Average Liquid ,
Sufam Temperature(psia): 0.0088
Vapor Pressure at Daily Minin um Liquid
Surface Temperature(psis): 0.0068 -
Vapor Pressure at Deily Maximum Liquid
Surface Temperaum(psia): 0.0117
-- Daily Avg.Liquid Surface Temp.(deg R): 528.1618
Daily Min Liquid Surface Temp.(deg Ry 517.6217 ..
Daily Max.Liquid Surface Temp.(deg R): 538.7018
Daily Ambient Temp.Range(deg.R): 21.7167
Vented Vapor S,tm Lion Fader
Vented Vapor Saturation Factor. 0.9994
Vapm Pressum at Daily Average Uquid:
_ Sudam Temperature(psi.): 0.008E -
Vapor Spam Outage(it): 12-IM
W.,Idng Losses(lby 0.8830
Vapor M.I-L rWoight(Ibllbmole): 130.0000
4 Vapor Pressure at Daily Average Liquid
Sells-Tertpe2Wm(play. 0.0088
An-Net Through put(g.Uyr.): 32,572.1405
Annual Turno-re, 31.6800
Turnover Factor: 1.000D
Maximum Liquid Volume(gap' 1,028.1610 ..
Maximum Liquid Heigh'(it). 7.DOW
Tank Diameter(ft): 5.0000
Working Lass Product Factor: 1.0000
.Total tosses Qby. 1.0202
file:///C:/Program%2OFiles/Tanks4O9d/summarydisplay.htm 6/12/2014

j TANKS 4.0 Report Page 5 of 6
TANKS 4.0.9d
Emissions Report-Detail Format
Individual Tank Emission Totals
Emissions Report for:Annual
Moncure-Diesel(1000 gallon)-Vertical Fixed Roof Tank
Moncure,North Carolina
- Losses(lbs)
Components 11 Working L-S11 Breathing LossIl Total Emissions -
Distillate fuel oil no.2 IF 0.88 E14]1 102
i
I .
i
I '
file:///C:/Program%2OFiles/Tanks4O9d/summarydisplay.htm 6/12/2014

TANKS 4.0 Report Page 1 of 6
TANKS 4.0.9d
Emissions Report-Detail Format
Tank Indentification and Physical Characteristics
Identfication
User Identffication: Moncure-Gasoline Tank(1000 gallon)
_ City: Moncure
State: North Carolina
Company. General Shale Brick
Type of Tank: Vertical Fixed Roof Tank
Description: El-1000 gallon gasoline tank
_ Tank Dimensions
Shell Height(ft): 8.00
Diameter(it): 5.00
Liquid Height(ft): 7.00
-- Avg.Liquid Height(ft): 7.00 -
Volume(gallons): 1,028.16
_ Turnovers: 2.67
Net Throughput(gaVyr): 2,745.19
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(it) 0.50
Radius(it)(Dome Roof) 0.00
Breather Vent Settings -
Vacuum Settings(psig): -0.03
Pressure Settings(psig) 0.03
Meterological Data used in Emissions Calculations:Raleigh,North Carolina(Avg Atmospheric Pressure=14.53 psia)
file:///C:/Program%2OFiles/Tanks4O9d/summarydisplay.htm 6/12/2014

TANKS 4.0 Report Page 2 of 6
TANKS 4.0.9d
Emissions Report-Detail Format
Liquid Contents of Storage Tank
Moncure-Gasoline Tank(1000 gallon)-Vertical Fixed Roof Tank
Moncure,North Carolina
Liquid
Daily Liquid Surf. Bulk Vapor Liquid Vapor
Temperaaae(deg F) Temp Vapor Preswm(Psia) Md. Mass Maw Mol. Basis(orVapor Pressure
MuNre/Component M-1h Avg. Min. Mae. (deg F) Avg. Min. Maa. Might, Fraa Fraa Weight CakaYa -
Gasoline(RVP 10) All 68.49 57.95 79.03 62.36 6.0979 4.9830 7.4035 66.L1000 92.00 Option 4:RVP=10.ASTM Slope=3
1
file:///C:/Program%2OFiles/Tanks4O9d/suimamarydisplay.htm 6/12/2014

TANKS 4.0 Report Page 3 of 6
TANKS 4.0.9d
Emissions Report-Detail Format
Detail Calculations(AP-42)
Moncure-Gasoline Tank(1000 gallon)-Vertical Fixed Roof Tank
Moncure,North Carolina
Armual Eniasim cakaWariore
Standing Losses(Ib): 163.3353 -
VaPor space Volurm(m ft): 24.fi091
Vapor Density(Ibtw It): 0.0710
Vapor Space Expanson Factor: 0.3598
Vented Vapor Saturation Factor. 0.7117
Tank Vapor Spam Volume:
Vapor Spam Volume(m ft): 24.6091
Tank Diameter(ft): 5.DODO
Vapor Spam Outage(ft): 1.2533
Tank Shell Height ft. 8.0000
- Average Liquid Height(ft): 7.0000
Roof Outage(ft): 0.25M
Roof Outage(Dome Roof)
Roof Outage(R): 0.25M
Dome Radius(fty ODOM
Shell Radius(h): 2.5000
Vapor Density
Vapor Density(Ib/m ft): 0.0710
Vapor MoI-W Weight(Ibllbmole): 66,0000
Vapor Pressure at Daily Average Liquid
Su=Temperature(psia): 6.0979
Daily Avg.Liquid Suns-Temp.(deg.R): 528.1618
Daily Average Ambient Temp.(deg.Fr. 59.2833
Ideal Gas Cone:tant R
(Psia tuft y(Ibm-.R)1 10.731
Liquid Bulk_r.""""(deg.R): 522,0333
Tank Paint Solar Absorpomm(Shell): 0.6800
Tank Paint Solar Aoao ptanm(Roof): 0.6800
Daily Total Solar Insulation
Factor(Bt fgft day): 1.393.0797
Vapor Spam Expansion Fedor
Vapor Spam Expansion Fa : 0.3598
Daily Vapor Temperature Range(deg.R): 42.1602
Daily Vapor Pressure Range(pia): 2A206
Breather Vent Press.Setting Range(psia): 0.0600
Vapor Pressure at Daily Average liquid
Surtam Temperature(psis): 6.0979
Vapor Pressure at Daily Minimum Liquid
Surtam Temperature(psia): 4.98W
Vapor Pressure at Daily Maximum Liquid
Sudam Temperature(psia): 7.4035
-- Daily Avg.Liquid Surface Temp.(deg R): 528.1618
Daily Min.Liquid Staf ce Temp.(deg R): 517.6217
Daily Max.Liquid Surface Temp.(deg R): 538.7018
Daily Ambient Temp.Range(deg.R): 21.7167
Vented Vapor-,Wmg,n Factor
Vented Vapor S xtumaon F.M.. 0.7117
Vapor Pressure at Daily Average Liquid:
Sudan Temperature(pia): 6.0979
Vapor Spam Outage(ft): 1.2533
Working Lomas(lb): 26.3056 '
- Vapor MoImWar Weight(Ib/lbmole): 66.0000
Vapor Pressure at Daily Average Liquid
Surface Temperature(psa): 6.0979
Annual Net Throughput(gagyr): 2.745.1899 '
Annual Tummers: 2.6700
- - Turnover Factor: 1.0000
Maximum LigWd Volume(gap: 1.028.1610
Maximum Liquid Height(ft): 7.0000
Tank Diameter(n): 5.0000
Working Loss Product Favor. 1.0000
I Total Losses(l6): 189.6409 '
file:///C:/Program%2OFiles/Tanks4O9d/summarydisplay.btm 6/12/2014

TANKS 4.0 Report Page 5 of 6
TANKS 4.0.9d
Emissions Report-Detail Format
Individual Tank Emission Totals
Emissions Report for:Annual
Moncure-Gasoline Tank(1000 gallon)-Vertical Fixed Roof Tank
Moncure,North Carolina
Losses(lbs)
Components 11 Working Loss I Breathing LossIl Total Emissions
Gasoline(RVP 10) IF 2631jj 1K.34]1 189.64
I
f
file:///C:/Program%2OFiles/Tanks4O9d/suminarydisplay.htm 6/12/2014

TANKS 4.0 Report Page 1 of 6
TANKS 4.0.9d
_ Emissions Report-Detail Format
Tank Indentification and Physical Characteristics
Identification -
User Identification: Moncure-Gear oil(350 gallons)
City: Moncure
State: North Carolina
Company. General Shale Brick
Type of Tank: Vertical Fixed Roof Tank
Description: El-Gear oil tank 350 gallons
Tank Dimensions
Shell Height(ft): 7.55
Diameter(ft): 3.00
Liquid Height(ft): 6.55
Avg.Liquid Height(ft): 6.55
Volume(gallons): 346.34
_ Turnovers: 1.73
Net Throughput(gaVyr): 550.69
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) 0.00
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)
file:///C:/Program�/�2OFiles/Tanks4O9d/summarydisplay.htm 6/12/2014

TANKS 4.0 Report Page 2 of 6 �I
� I
TANKS 4.0.9d J
Emissions Report-Detail Format
Liquid Contents of Storage Tank
Moncure-Gear oil(350 gallons)-Vertical Fixed Roof Tank -'
Moncure,North Carolina
Ligrid
Daily Liquid Be. Bulk Vapor Liquid Vapor
TemperaMe(deg F) Temp Vapor Pressur.(Paw) Mal Mass Maas Me]. Basis for Vapor Presswa
MixWre/ComporeM Monts Avg. Min. Maz. (deg F) Avg. Min. Mai VkgfR F2U. Frac[ Weight CakWanans --
Crud.of(RVP 5) AA 68.49 57.95 79.03 6236 3.3910 2.7639 4.1272 50.0000 207.00 Option 4:RVP=S
i
file:///C:/Program%2OFiles/Tanks4O9d/summarydisplay.htm 6/1-2/201.4

TANKS 4.0 Report Page 3 of 6
i
TANKS 4.0.9d
Emissions Report-Detail Format
Detail Calculations(AP-42)
Moncure-Gear oil(350 gallons)-Vertical Fixed Roof Tank
Moncure,North Carolina
A-]Emission CakaWations- --
Standng Losses Ob): 15.6000
Vapor Space Vokme(ou fly: 8.9012
Vapor Density(lb/m O): 0.0299'
Vapor Spam Exparvan Factor: 0.1968
Vented Vapor Saturation Factor. - 0.8155
Tank Vapor Spam Volume:
Vapor Spam Volume(m ft): 8.9012
Tank D'ametor(8): 3.0000
Vapor Spam Outage(R): 1.25M
I Tank Shell Heigh(tty 7.SSW
Avenge L'pad He Or): 6.SSW
RoofOutage(ft): 02593
Roof Outage(Dome Roof)
Root Outage(8): 02593
Dom RaSus(tty 0.00DO
Shall Radm(8): 1.5000
F Vapor Density -
Vapor Density(INcu R): 0.0299
Vapor M.1ow.r Weight(lbo b-mole): 50.0000 -
Vapor Pressure at Daily Avenge Liquid
- Surface Temperature(psia): 3.3910
Daily Avg.Liquid Sudan Temp.(deg.R): 528.1618
Daily Average Ambient Temp.(doo.FL 59.2833
.at Gas Constant R
-(psia adt I(r-ldeg R)) 10.731
Liquid Bulk Temperature(deg.R): 522.0333
Tank Paint Solar Abamptarm(Shell): D.6BW
To
Paint Solar Absorym m W tae(RQ: O.68
_- Daily Total Solar Insulation
Factor(BttdsgB dayy. 1.393.0797
Vapor Spam Expansion Factor '
Vapor Spam Expansion F.c . 0.1968
Daily Vapor Temperature Range(deg.R): 42.1602
Daily Vapor Prossua Range(psiar 1.3633
Breather Vent Press.Setting Range(psia): 0.0600
Vapor Presue at Daily Average Liquid
Surface Temperature(psi.): 3.3910 -
Mope r Presua at Daily Minimum Liquid
Surace Temperature(psi,): 2.7639
Vapor P.-at Daily Maormmr UWkf
Sudan Temperature(pia): 4.1272
Daily Avg.Liquid Surface Temp.(deg R): 528161E
Daily Min.Liquid Surface Tamp.(deg R): 517:6217
Daily Max.Laud Sudan Tang.(deg R): 538.7018
Daily Ambient Temp.Range(deg.R): 21.7167
Vaned Vapor SatureVon Factor
Vented Vapor Saturtion Factor: 0.8155
Vapor Pressure at Daily Avenge Liquid:
Sudan Temperature(psia):. 3J910 r
Vapor Spam Outage(0): 12593
V%d.V Loses(Ib): 1.6673
Vapor Moluedar Weigfd Vlxlb�nole): 50.0000
Vapor Pressure at Daily Avenge Liqu'd
Sudan Temperature(psia): 3.3910
Annual Net Ttvoughprd(gatlyrJ: 550.6BSO
Annual Trarovens 1.7300
-- Tumovet Factor: 1.0000
Maximlan Liquid Volume(gale 346.3434
Maximus Liquid Height(d): 6.5500
Tank D'armbr(8): 3.DOW
VWddng Loss Product Fao . 0.7500
Total Losses(IbX 17.2679 -
file:///C:/Program%20Files/Tanks4O9d/su'mmarydisplay.htm 6/12/2014

TANKS 4.0 Report Page 5 of 6
TANKS 4.0.9d
Emissions Report-Detail Format
Individual Tank Emission Totals
Emissions Report for:Annual
Moncure-Gear oil(350 gallons)-Vertical Fixed Roof Tank
Moncure,North Carolina
Losses(lbs)
Components Working LoSS11 Breathing Loss I Total Emissions
Crude ail(RVP 5) 1.67
J1 15.601 17.27
V
file:///C:/Program%2OFiles/Tanks4O9d/summarydisplay.htm 6/12/2014

TANKS 4.0 Report Page 1 of 6
TANKS 4.0.9d
Emissions Report-Detail Format
Tank Indentification and Physical Characteristics
- Identification
User Identification: Moncure-Motoroil(160 gallon)
_ City. Moncure
State: North Carolina
Company: General Shale Brick
Type of Tank: Vertical Faed Roof Tank
Description: El-Motor oil tank 160 gallons -
-_ Tank Dimensions
1 Shell Height(11): 5.50
Diameter(it): 2.50
Liquid Height(it): 4.50 -
-- Avg.Liquid Height(ft): 4.50
Volume(gallons): 165.24
Turnovers: 1.28
- Net Throughput(gaLfyr): 211.51
! 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(it) 0.50 -
Radius(ft)(Dome Roof) 2.50
Breather Vent Settings
Vacuum Settings(psig): -0.03
Pressure Settings(psig) 0.03
Meterological Data used in Emissions Calculations:Raleigh,North Carolina(Avg Atmospheric Pressure=14.53 psia)
r
li
file:///C:/Program%2OFiles/Tanks4O9d/summarydisplay.htm 6/12/2014

TANKS 4.0 Report Page 2 of 6.
TANKS 4.0.9d
Emissions Report-Detail Format
Liquid Contents of Storage Tank
Moncure-Motor oil(160 gallon)-Vertical Fixed Roof Tank
Moncure,North Carolina
Liquid
Daily Liquid Surf. BWk Vapor Liquid Vapor
TemperaE e(deg F) Temp Vapor Presmre(Psa) M.I. M.- Maw Md. Bass tor Vapor Premua
MixWre/Compmwrd Month Avg Mil Max. (deg F) Avg. Min. Max. Might FracL Fraet might C'Iculatioss
Crude od(RVP 5) ---_—`AD 68.49 57.95 79.03 62.36 3.3910 Z7639 4.1272 50.0000—--._ _--- 207.00 Op ion 4:RVP--S
1
file:///C:/Program%2OFiles/Tanks4O9d/summarydisplay.htm . 6/12/201.4

TANKS 4.0 Report Page 3 of 6
TANKS 4.0.9d
Emissions Report-Detail Format
Detail Calculations(AP-42)
Moncure-Motor oil(160 gallon)-Vertical Fixed Roof Tank
Moncure,North Carolina
Amual rni-Cakauarions^_-
Standing Losses(lb): 10.8623
Vapor Space Volume(m fq: 62014
Vapor Density(Ibfm fl): 0.0299
Vapor Space Expansion Factor. 0.196E
Vented Vapor Saturation Fader. 0.8150 -
Tank Vapo,Spam Volume:
Vaporspace Volume(a1 fl): 62014
•I Tank Diameter(R): 2.5000
Vapor Spam Ourage(8): USW
Tank Shell Height(Ry 5.SOW
Menage Liquid Height(8): 4.5000
Roof Outage(8): 02633
Roof Outage(Dome Pool) _
Roof Outage MY 0.2633
Dome Radius(ft): 2.5000
Shot]Radius(8): 12500 _
Vapor Density .
Vapor Density(Idar 8): 0.0299
Vapor Molecular Weight(Iblltrmole): 50.0000 -
Vapor Pressure al Daily Avenge Liquid
Sudan Temperature(Psi.): 33910
Daily Avg.Liquid Surface Temp.(deg.R): 528.1618
Da9y Average Ambient Temp.(deg.Fy 59-IM
Ideal Gas Constant R
(Psia dull y(bnaldeg R)): 10.731
Liquid Bulk Temmature(deg.R): 522.0333
Tank Paint Salar Absorpemoo(Shell): 0.6800 -
Tank Paint Sob,Absorpb,-(R-9: 0.6800
Daay Total Sol.,Irsulatian
F.-(Btu/sgft day): 1.3.g3.0797
Vapor Spam Expansion Factor
Vapor Spam Expansion Fader. 0.1968
Daily Vapor Temmralme Range(deg.R): 42.1602
Daily Vapor Pressure Range(psia): 1.3633
Breather Vent Press.Setting Rangs(psia): 0.0600
Vapor Pressure at Daily Average Liquid
Surface Temperature(psi.): 3.3910
Vapor Pressure at Daily Minimum Liquid
Sudace Temperature(pia): 2.7639
Vapor Pressure at Daly Max-Liquid
Surface Temperature(pia): 4.1272
Daily Avg.Liquid Surface Temp.(deg R): 528.1618
Daily Min.Liquid Sudan 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 Fader
Vented Vapor Satuatem Fedor. M8150
l Vapor Pressure at Daily Average Liquid:
Sudan Tern"mtum(psi,): 3.3910
Vapor Space Outage(R): 1.2633
Working losses(lb): 0.6404
Vapor Mold ar Weight(Ibgbmde): 50.0000
Vapor Pressure at Daily Average Liquid
Surface Temperature(pia): 3.3910
Anmral Net Throughput(gaVyr.): 211.6074
1. Annual Turnovers: 128M
Turnover Fatter. 1.0000
Maxtmum Liquid Volume(g,q: 165.2402
Maximan Liquid Height(k): 4.5000
Tank Diameter(8): 2.5000
Wading less Product Factor. 0.7500
Total Losses(Ib): 11.5027
file:///C:/Program%2OFiles/Tanks4O9d/summarydisplay.htm 6/12/2014

TANKS 4.0 Report Page 5 of 6
TANKS 4.0.9d
Emissions Report-Detail Format
Individual Tank Emission Totals
Emissions Report for:Annual
Moncure-Motor oil(160 gallon)-Vertical Fixed Roof Tank
Moncure,North Carolina
Losses(lbs)
Components Working L—o—ssll Breathing Loss]j Total Emissions
Crude oil(RVP 5) IF0.64 10.86 11.50
f
file:///C:/Program%2OFiles/Tanks4O9d/summarydisplay.htm 6/12/2014

TANKS 4.0 Report Page 1 of 6
TANKS 4.0.9d,
Emissions Report-Detail Format
Tank Indentification and Physical Characteristics
--- Identification
User Identification: Moncure-Waste oil(275 gallon) _
_ City: Moncure
State: North Carolina
Company: General Shale Brick
Type of Tank: Vertical Fixed Roof Tank
Description: EI-Waste oil Tank 275 gallons
_ Tank Dimensions
Shell Height(ft): 6.25
' Diameter(it): 3.00
Liquid Height(it): 5.25
- Avg.Liquid Height(ft): - 5.25
Volume(gallons): 277.60
Turnovers: 2.22
Net Throughpul(gallyr): 61626
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(it) 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)
file:///C:/Program%20Files/Tanks4O9d/summarydisplay.htm 6/12/2014

TANKS 4.0 Report Page 2 of 6
TANKS 4.0.9d
Emissions Report-Detail Format
Liquid Contents of Storage Tank
Moncure-Waste oil(275 gallon)-Vertical Fixed Roof Tank
Moncure,North Carolina
Liquid
Oagy Liquid Surf. Bulk vapor Liquid vapor
Temperature(deg F) Temp Vapor Pressure(psia) MOL Mara Mass M.I. Basis fur Vapor Preseue
whoa Component Month Avg, Min. Max. (deg F) Avg. Min. Max. Weight Fret F..L Weight Calculations
Residual oil no.6 Ag 68.49 67M 79.03 6238 0.0001 MOODD 0.0001 190.0000 387.00 Option 1:VPGO=.00004 VP70=.00006
{
file:///C:/Program%2OFiles/Tanks4O9d/summarydisplay.htm 6/12/2014

TANKS 4.0 Report Page 3 of 6
_ TANKS 4.0.9d
Emissions Report-Detail Format
Detail Calculations(AP-42)
Moncure-Waste oil(275 gallon)-Vertical Fixed Roof Tank
Moncure,North Carolina
Annual Emission Calmutatieru
Standing Loses(lb): 0.0005
Vapor Space Volume(w ft): a.9012
Vapor Density QWw ft): O.00w
Vapor Space Expansion Factor. 0.0757
Vented Vapor Saturation Factor: 1.0000
Tank Vapor Spew Volume:
Vapor Spew Volumxt(eu n 6.9012
Tank Diameler(ft): 3.0000 -
Vapor Spam Outage(ft): 12593
Tank Shell Height(ft). 6.2500
Average Liquid Height(ft): 5250D
Roof Outage(it): 0.2593
Roof Outage(Dorm Roof) .
Roof Outage(By. 02593
Dorm Radius Mk 3.0000
Shell Radius(ft): 1.5000
Vapor Density
Vapor Density(lblw h): 0.0000
Vapor Mok War N6ight(INibmole): 190.0000
Vapor pressure at Daily Average Liquid
Sudm a Temperature(psia): 0.0001
OadyAvg.Liquid Surface Temp.(deg.R): 52B.1618
Daily Avenge Ambiibienl Temp(deg.F): 592833
Ideal Das Constant R
(pia cult(b-IEeg R)): 10.731
-- Liquid Bulk Temperature(deg.R): 522.0333
Tank Paint Sala,Absorpta=(Shall): 0.6800
Tank Pamt Solar Abserptanxxf(Roof): 0.6800
Daily Total Solar Insuiation
Factor(Btulsgft day): 1.393.0797
Vapor Space Expansion Factor
Vapor Space Expensim Factor. 0.0757
D. Vapor Temperature Range(deg.R): 42.1602
Daily Vapor Presure Range(psla): 0.0000
Breather Vem press.Setting Range(psia): 0.0600
Vapor Presuree at Daily Average Liquid
Surface Temperabm(psia): 0.0001
Vapor Pressure el Daily Minimum Liquid
Sudam Temi arab,e(psi.): 0.0000
Vapor P essun,at Daily Marirwrtn liquid
Surface Tamparatu.(psi.): 0.0001
Daily Avg.Liquid Surface Temp.(deg R): 52B.1618
Daily Min.Liquid Surface Temp.(deg Rr 517.6217
Daily Max.Liquid Surface Temp.(deg R} 538.7018
Daily AmHerd Temp.Range(deg.R): 21.7167
Vented Vapor Saturation Factor
Vented Vapor Saturation Factor: 1.OD00
Vapor Pressue at Daily Average Liquid:
Surface Temperature(psi.): 0.0001
Vapor Spam Outage(ft): 1.2593
VWddng Losses(b): 0.0002
Vapor MOO W e):ar Weight 190.0000
Vapor Preswe at Daily Average LkVM
Surface Temperature(psia): 0.0001
Annual Net Throughput(gaVyrj: 6162797
Annual Turnovers 22200
Tummver Factor: 1.000D
Maniman Liquid V.I-(gal): 271.6035
Maximum Liquid Height(ft): 52500
_ Tank Dbmetar(fly. 3.0000
Worlurg Loss product Factor: 1.003D
Total Losses(lby 0.0006
file:///C:/Program%2OFi.les/Tanks4O9d/summarydisplay.htm 6/12/2014

TANKS 4.0 Report Page 5 of 6
_ TANKS 4.0.9d
Emissions Report-Detail Format
Individual Tank Emission Totals
Emissions Report for:Annual
Moncure-Waste oil(275 gallon)-Vertical Fixed Roof Tank
Moncure,North Carolina
Losse4bs)
Components Working lm—sj Breathing Lossll Total Emissions
Residual oil no.6 0.00 0.0011 0.00
i
i
file:///C:/Program%2OFiles/Tanks4O9d/summarydisplay.htm 6/12/2014

I
Dana Nowell
From: [e-mail]
- Sent: Thursday, June 19, 2014 4:47 PM
Subject: Inventory submission confirmation -- 1900009
Dear Dana Norvell
Your submittal of the 2013 emission inventory for General Shale Brick, Inc. Moncure Facility, 1900009, has been
received by the North Carolina Division of Air Quality(DAQ)on June 19,2014 at 16:46*44.You have until the due date of
the emission inventory or two weeks from this submittal to review and repudiate the data submitted.
Please remember to:
-print the Certification Form (see AERO Closeout page),
-have the Responsible Official sign it in blue ink,
-include copies of spreadsheets or calculations used in creating this inventory, and
-mail (postmark) it to NCDAQ, 3800 Barrett Drive, Raleigh, NC 27609 by the required due date in order for this
submittal to be considered complete. If you have any questions, please feel free to contact Will Wike, in the Raleigh
Regional Office,at919-791-4200.
The Division of Air Quality thanks you for using AERO, the on line emissions inventory program.
Sincerely
DAQ
i
l -
1