AQ_F_0400052_20210610_EI_Apprd-EI

2020 Emissions Inventory Review / Data Tracking Form
Facility Name: Anson County Waste Management Facility Facility ID: 0400052
Facility Assigned to: Data Entry: Anson County
Classification: Jeffrey D. Cole Confidential Copy Submitted?
Title V ❑ YES
NO
Initial Review/ Data Entry
0 Enter date received into ED. Date Received: 06/10/2021
0 Assigned to appropriate individual. Date Assigned: 06/10/2021 Date Due: 08/10/2021
❑ Paper copy submitted: One copy received with supporting documentation, certification form signed by responsible
official,and appears generally complete;OR
0 Electronic copy submitted: All supporting documentation and certification form(with time/date stamp)signed by
responsible official has been received.
Comments:
Inventory Review
0 All forms and supporting documentation appear to be complete if paper submission(check ED OS data if electronic).
0 Contact,address,phone number changes entered into I-Beam/Facilities if necessary.
0 All known operating scenarios,control devices,and emission release points have been entered for each emission
source(permitted,insignificant,and unpermitted)or note that the emission source was not operated or not required to report.
0 Check if SCC codes for each OS are accurate and update if needed.
0 Evaluate"U"sources for significance and address according to policy.
0 Calculations/forms appear to add up correctly.
0 All compliance issues are being addressed(e.g.Toxics limits,above TV thresholds, large emissions
increase/decrease, installation without a permit).
0 All volatile HAPs/TAPs were included in the VOC total.
0 Calculations and control efficiencies appear correct. Emission factors are the best available and most current factors
appropriate for the reporting facility(e.g. stack testing,AP-42,etc.).
0 Review facility comments and address any issues.
0 Update ED(Data Entry Main) if additional information is required(corrections due date and date received).
0 Check all ED QA/QC reports.
0 Comparison with previous emission inventory must be made and outliers(> 10%)must be investigated and explained.
0 Put inventory review comments and summarize any changes in ED-Data Entry Main"DAQ internal comments".
Date Info Requested: Date Info Received: Total Days on Hold:
Date Review Complete: _07/16/2021 Signature:
Date Submitted to EI Coordinator: 07/16/2021
Date Approved: 07116/2V21 Initials: (;2Ujc?

Facility Total CY 2020 Emission Summary Recorded in ED Facility ID #: 0400052
Facility Name: Anson County Waste Management Facility Permit#(s): 09835T04
Green House Gases Pollutants (GHG) Actual Emissions
Tons/Yr
Pollutant CAS CY 2020 CY 2019 Demini- Change
from ED from Fees mus
Nitrous Oxide (N20) 10024972 Not Not 1.0 N/A
Reported Reported
Methane (CH4) 74-82-8 Not Not 10.0 N/A
Reported Reported
Carbon Dioxide (CO2) 124389 Not Not 59000.0 N/A
Reported Reported
CO2 equivalent(sum of individual GHG pollutant emissiot No GHGs
times their 1995 IPCC Global Warming Potential (GWP), Reported
converted to metric tons)
Criteria Pollutants Actual Emissions
(Tons/Year)
Pollutant CAS CY 2020 CY 2019 Demini- %
from ED from Fees mus Change
CO co 39.06 29.65 0.5 31.7%
NOx NOx 7.18 5.45 0.5 T1.7%
PM(TSP) TSP 1.77 1.34 0.5 32.1%
PM10 PM10 1.77 1.34 0.5 32.1%
PM2.5 PM2.5 1.77 1.34 0.5 32.1%
S02 SO2 1.20 0.910000 0.5 31.9%
VOC voc 3.76 3.81 0.5 -1.3%
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPs) (Pounds/Year)
Pollutant CAS CY 2020 CY 2019 Demini- %
from ED from Fees mus Change
Mercury & Compounds-all total mass includes Hg Vapor 0.056090 0.056940 0.001 -1.5%
Mercury, vapor(Component of HGC) 7439-97-6 0.056090 0.056940 0.001 -1.5%
Total Reduced Sulfur (TRS as total mass) 829.09 841.42 -1.5%
Hydrogen sulfide 7783-06-4 769.57 781.00 1.0 -1.5%
Methyl mercaptan 74-93-1 59.52 60.41 1.0 -1.5%
Acrylonitrile 107-13-1 2.27 2.40 10.0 -5.2%
07/16/2021 Page 1 of 4

Facility Total CY 2020 Emission Summary Recorded in ED Facility ID #: 0400052
Facility Name: Anson County Waste Management Facility Permit#(s): 09835T04
Hazardous Air Pollutants (HAPs) Actual Emissions
and/or Toxic Air Pollutants (TAPs) (Pounds/Year)
Pollutant CAS CY 2020 CY 2019 Demini- %
from ED from Fees mus Change
Benzene 71-43-2 72.70 73.79 1.0 -1.5%
Bromoform 75-25-2 0.444020 0.540610 10.0 1 -17.9%
Carbon disulfide 75-15-0 23.77 24.22 10.0 -1.8%
Carbon tetrachloride 56-23-5 1.03 1.05 1.0 -1.5%
Carbonyl sulfide 463-58-1 10.53 10.68 1.0 -1.5%
CFC-11 (Trichlorofluoromethane) 75-69-4 0.444020 0.540610 100.0 1 -17.9%
CFC-12 (Dichlorodifluoromethane) 75-71-8 202.74 205.78 100.0 -1.5%
Chlorobenzene 108-90-7 24.47 24.84 10.0 -1.5%
Chloroform 67-66-3 2.84 2.98 100.0 -4.5%
Dichlorobenzene(p), 1,4- 106-46-7 226.24 229.64 1.0 -1.5%
Dichloropropene, 1,3- 542-75-6 0.444020 0.540610 1.0 -17.9%
Ethyl benzene 100-41-4 690.19 700.54 100.0 -1.5%
Ethyl chloride (chloroethane) 75-00-3 15.21 15.53 10.0 -2.0%
Ethyl mercaptan 75-08-1 80.68 81.89 10.0 -1.5%
Ethylene dibromide (dibromoethane) 106-93-4 8.28 8.40 1.0 -1.5%
Ethylene dichloride (1,2-dichloroethane) 107-06-2 11.37 11.54 1.0 -1.5%
Ethylidene dichloride (1,1-dichloroethane) 75-34-3 70.67 71.82 100.0 -1.6%
Hexane, n- 110-54-3 191.79 194.66 100.0 -1.5%
Hydrogen chloride (hydrochloric acid) 7647-01-0 1,236.02 938.29 100.0 31.7%
MEK(methyl ethyl ketone, 2-butanone) 78-93-3 729.43 740.45 100.0 -1.5%
Methyl bromide (bromomethane) 74-83-9 0.444020 0.540610 1.0 -17.9%
Methyl chloride (chloromethane) 74-87-3 12.48 12.76 1.0 -2.2%
Methyl chloroform 71-55-6 21.47 21.80 100.0 -1.5%
Methyl iodide (iodomethane) 74-88-4 0.444020 0.540610 10.0 1 -17.9%
i
Methylene chloride 75-09-2 276.15 280.28 1.0 -1.5%
MIBK(methyl isobutyl ketone) 108-10-1 72.38 73.55 10.0 -1.6%
07/16/2021 Page 2 of 4

f
Facility Total CY 2020 Emission Summary Recorded in ED Facility ID #: 0400052
FacilityName: Anson Coun Waste Management Facili Permit#(s): 09835T04
tv � tv
Hazardous Air Pollutants HAPs Actual Emissions
and/or Toxic Air Pollutants (TAPs) (Pounds/Year)
Pollutant CAS CY 2020 CY 2019 Demini- %
from ED from Fees mus Change
Perchloroethylene (tetrachloroethylene) 127-18-4 189.45 192.29 100.0 -1.5%
Propylene dichloride (1,2-dichloropropane) 78-87-5 2.49 2.53 10.0 -1.5%
Styrene 100-42-5 0.004440 0.005410 100.0 1 -17.9%
TCE (trichloroethylene) 79-01-6 85.69 86.97 1,000.0 -1.5%
Tetrachloro-2,2-difluoroethane, 19191,2- (CFC 112a) 76-11-9 0.444020 0.540610 1,000.0 1 -17.9%
Tetrachloroethane, I,1,2,2- 79-34-5 11.70 11.96 100.0 -2.2%
Toluene 108-88-3 2,241.37 21274.97 100.0 -1.5%
Trichloroethane, 1,1,2- 79-00-5 0.000220 0.000270 100.0 N/A
Vinyl chloride 75-01-4 64.46 65.42 0.1 -1.5%
Vinylidene chloride 75-35-4 8.98 9.21 0.1 -2.4%
Xylene (mixed isomers) 1330-20-7 1,686.16 1,711.51 100.0 -1.5%
Largest Individual HAP Toluene 2,241.37 lbs
Total HAP Emissions 7,262.01 lbs
Largest Individual CAP CO 39.06 tons
Total CAP Emissions 52.97 tons
Total TAP Emissions 8,098.31 lbs
Total Aggregate 54.23 tons
Emissions
07/16/2021 Page 3 of 4

DAQ's Comments Regarding Inventory
The increases in all criteria emissions and HCL emissions,except VOC emissions,can be directly tied to the fact that this landfill se
more gas to flare in 2020,therefore the emissions from the flare increased. In 2019,sent 317 mm scf to flare and 2020,sent 417 mn
to Flare. In 2020 collection increased from 2019 by 33.7%. The landfill collected more gas in 2020,therefore,the emissions from
fugitive decreased. Also,the capture efficiency of the landfill was estimated at 54%in 2020 vs 46.6%in 2019. When your overall
capture efficiency increases more gas goes to flare so the landfill VOC emissions would decrease as more gas goes to the flare wher
it is better controlled through combustion. There are a number of HAPs that show a 17.9%reduction between 2019 and 2020
however these annual value differences are very small(0.00541 lbs/yr vs.0.00444 lbs/yr,each).They are accountable by a 17.9%
reduction in the amount of leachate processed. Note also that this landfill tested out of the requirements of a GCCS and only
operates a Voluntary GCCS per NSPS WWW.
07/16/2021 Page 4 of 4

COPY of RECORD Date Submitted: 6/3/2021 11 :57:49
Inventory Certification Form(Title V)
Facility Name: Anson County Waste Management Facility Facility ID : 0400052
375 Dozer Drive Permit : 09835
Polkton,NC 28135 County : Anson
DAQ Region : FRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory-Calendar Year 2020
These forms must be completed and returned even if the facility did not operate or emissions were zero
The legally defined "Responsible Official" of record for your facility is Tyler Fitzgerald
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 pen-nit 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 proprietorship;a general partner or the proprietor,respectively;
3. For a municipality,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:
(Important: Legally Responsible Official,read and sign after all submissions are final.)
I certify that I am the responsible official for this facility,as described above,and hereby certify that the information contained in
this air emissions report, including attached calculations and documentation, is true, accurate and complete. (Subject to legal
penalties 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 (us blue ' k . Date Signed:
Printed Name: Tyler Fitzge ld
Signature:
This form applies to Title V facilities. If this facility is not classified asTitle V,please telephone your regional office Emission
Inventory Contact at once for proper forms.
Email address of Responsible Official: [e-mail]
Information on this Form cannot be held confidential
COPY of RECORD Date Submitted: 6/3;2021 11:57:49
1

(45
a4RECEIVED Franklin Engineers&Consultants,LLC.
n Frkift. 2734 Sunrise Blvd,Suite 308
Pearland,TX 77584
Engineers&Consultants,LLC. ,JUN 10 2021 Phone: [phone]
DEa-FAYETTEVILLE REG4OML OFFICE
June 8,2021
Joshua Harris Environmental Engineer
North Carolina Department of Environment of Environmental Quality—Division of Air Quality
Fayetteville Regional Office
Systel Bldg.
225 Green Street,Suite 714
Fayetteville,NC 28301-5094
RE: Anson County Waste Management Facility,Polkton,North Carolina
RY2020 Annual Emissions Report Certification and Back-up Calculations
Air Quality Permit No.9835T03 Facility ID:0400052
Dear Mr.Harris:
On behalf of Anson County Waste Management Facility(ACWM),Franklin Engineers&Consultants,LLC.
(FE&C)is pleased to submit the attached Responsible Official(RO)Certification and supporting calculations as a
follow-up to Air Emissions Reporting On-Line(HERO)submitted on 6/3/2021.
It should also be noted that a copy of the Responsible Official Change Letter submitted in 2016 is included as
Attachment C of this correspondence. If you have any questions regarding this resubmission,please contact Lana
Brown at(901)500-1812 or me at(281)205-8415.
Sincerely,
Franklin Engineers&Consultants,LLC.
Juene Franklin,P.E.
President
Attachments: Attachment A—Responsible Official Certification
Attachment B—RY2020 Emissions Inventory Supporting Calculations
Attachment C—Responsible Official Change Letter
cc: w/attachments
Lana Brown—Waste Connections Environmental Compliance Specialist(Electronic)
Tyler Fitzgerald—Waste Connections Assistant District Manager(Electronic)

COPY of RECORD Date Submitted: 6/3/2021 11:57:49
As entered in AERO
Facility Name: Anson County Waste Management Facility Facility ID : 0400052
375 Dozer Drive Permit : 09835
Polkton,NC 28135 County : Anson
DAQ Region : FRO
Listing of Emission Sources and Control Devices on Permit.See instructions
*ES ID on *ES Description *CS ID *CS Description *CD ID's
Air Permit
One municipal solid waste landfill Candle stick type flare(2500 scfm,75 million
ES-1 [NSPS XXX] CS-3 Btu per hour heat input(a)500 Btu/ft3 heat rate CD-1,GCCS-1
of landfill gas,Gas collection system,
Two Diesel fuel above ground
IES-2A storage tanks(12,000 gallon capacity CS-1 Flare CD-1
each)
Gasoline above ground storage tank
IES-3B (500 gallon capacity)[GACT
CCCCCC]
IES-4A Two leachate above ground storage
tanks(250,000 gallon capacity each)
2

COPY of RECORD Date Submitted: 6/3/2021 11:57:49
As entered in AERO
Facility Name: Anson County Waste Management Facility Facility ID : 0400052
375 Dozer Drive Permit : 09835
Polkton,NC 28135 County : Anson
DAQ Region : FRO
Emission Source& Operating Scenario List-See Instructions
'DES Group ID *ES ID SOS ID *OS Description
4 NONE
ES-1 LFG Emissions from landfill waste mass
6 and the control device(CD-1)
IES-2A 2 Municipal solid waste landfill
5 Fugitive emissions from the diesel tanks
IES-313 8 Fugitive Emissions from gasoline tank
IES-4A 7 Fugitive VOC emissions from leachate
tanks.
3

COPY of RECORD Date Submitted: 6/3/2021 11:57:49
As entered in AERO
Facility Name: Anson County Waste Management Facility Facility ID : 0400052
375 Dozer Drive Permit : 09835
Polkton,NC 28135 County : Anson
DAQ Region : FRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory-Calendar Year 2020
1.Emission Source ID(from permit) ES-1
or Emission Source Group ID
2. Emission Source Description : One municipal solid waste landfill [NSPS, Subpart WWW]
3. Operating Scenario ID/ OS-4/
Description:
4. SCC Number/Description: Not required by facility,will be completed by DAQ
5. Throughput/units in 2020:
(e.g.production or fuel use):
6. Fuel Information %Sulfur %Ash Heat Content
(If fuel is used)
(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 permit)
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 9): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
(in 0.1 feet)
ERT1 FUGITIVE(NO 1 72 Area= 1 Fugitives from
STACK) landfill waste mass
4

Operating Scenario: OS-4 Emission Source/Group ID: ES-1
10.Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2020)
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 Throughput:
Jan-Feb+Dec 25% March-May 25% June-Aug. 25% Sept.-Nov. 25%
2020 2020 2020 2020
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
Pollutants Pollutants Method Code (Net after Factor Control
(Tons/-"ear) (See Instructions) all controls)
2020
Criteria Emissions- Emission Control
Pollutant Emission Ef
(NAAQS) Criteria Estimation Efficiency
Pollutants Code Pollutants Method Code (Net after Factor Control
(Tons/Year) (See Instructions) all controls)
2020
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
Emissions Emission Control
(Net after all controls)
HAP/TAP CAS Estimation Emission EF
Pollutants(In Alphabetical order) (see instructions) HAP/TAPS Method Code Efficiency
f pounds/Y"ear) Factor Control
(See Instructions)
2020
5

COPY of RECORD Date Submitted: 6/3/2021 11:57:49
As entered in AERO
Facility Name: Anson County Waste Management Facility Facility ID : 0400052
375 Dozer Drive Permit : 09835
Polkton,NC 28135 County : Anson
DAQ Region : FRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory-Calendar Year 2020
1.Emission Source ID(from permit) ES-1
or Emission Source Group ID
2. Emission Source Description : One municipal solid waste landfill [NSPS, Subpart WWW]
3. Operating Scenario ID/ OS-6/LFG Emissions from landfill waste mass and the control device
Description: (CD-1)
4. SCC Number/Description: 50300601/Landfill Dump ; Waste Gas Flares
5. Throughput/units in 2020: 417279580 FT3S/yr
(e.g.production or fuel use):
6. Fuel Information %Sulfur %Ash Heat Content
(If fuel is used)
(Btu/units)
7. Capture Efficiency
(%of Emissions from this Process Vented 54
to Control Device or Stack):
8.Control Device Information
Order CS-ID CD ID Control Device Description
(as listed in permit)
1 CS-3 CD-1 Candle stick type flare(2500 scfm, 75 million Btu per hour heat input
at 506 Btu per cubic foot heat rate of landfill gas
2 CS-3 GCCS-1 Gas collection and control system
9.Emission Release Point(ERP)Information:(Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
(in 0.1 feet)
CD-1 VERTICAL 35.11 1 130 53.05 2500 Candlestick flare
STACK
6

1
Operating Scenario: OS-6 Emission Source/Group ID: ES-1
10.Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2020)
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 Throughput:
Jan-Feb+Dec 25% March-May 25% L2O
ne-Aug. 25% Sept.-Nov. 25%
2020 2020 20 2020
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
Pollutants Pollutants Method Code (Net after Factor Control
(Tons/Year) (See Instructions) all controls)
2020
Criteria Emissions- Emission Control
Emission Ef
Pollutant
(NAAQS) Criteria Estimation Efficiency
Pollutants Code Pollutants Method Code (Net after Factor Control
(Tons,Year-) (See Instructions) all controls)
2020
CO CO 39.06 08 0
NOx NOx 7.18 08 0
TSP TSP 1.77 08 0
PM10 PM10 1.77 08 0
PM2.5 PM2.5 1.77 08 0
S02 S02 1.2 1 08 0
VOC VOC 3.59 08 98 AFTER
Emission
HAP/TAP CAS Emissions Estimation Control Emission EF
Pollutants(In Alphabetical order) (see instructions) HAP/TAPS Method Code Efficiency Factor Control
(Pounds/Year) (Net after all controls)
(See Instructions)
2020
Acrylonitrile 107-13-1 1.82917 08 0
Benzene 71-43-2 72.70401 08 0
CFC-12 75-71-8 202.73737 08 0
(Dichlorodifluoromethane)
Carbon disulfide 75-15-0 23.32874 08 0
Carbon tetrachloride 56-23-5 1.03122 08 0
Carbonyl sulfide 463-58-1 10.52675 08 0
Chlorobenzene 108-90-7 24.46783 08 0
Chloroform 67-66-3 2.40089 08 0
Dichlorobenzene(p), 1,4- 106-46-7 226.21357 08 0
Ethyl benzene 100-41-4 690.16379 08 0
Ethyl chloride 75-00-3 14.7665 08 0
(chloroethane)
Ethyl mercaptan 75-08-1 80.6764 08 0
Ethylene dibromide 106-93-4 8.27606 08 0
Ethylene dichloride(1,2- 107-06-2 11.37173 08 0
dichloroethane)
Ethylidene dichloride(1,1- 75-34-3 70.2275 08 0
dichloroethane)
7

Hexane, n- 110-54-3 191.79093 08 0
Hydrogen chloride 7647-01-0 1236.01935 08 0
(hydrochloric acid)
Hydrogen sulfide 7783-06-4 769.57055 08 0
Mercury,vapor 7439-97-6 0.05609 08 0
(Component of HGC)
Methvl chloride 74-87-3 12.03899 08 0
Methyl chloroform 71-55-6 21.46264 08 0
Methyl ethyl ketone 78-93-3 728.98983 08 0
Methyl isobutyl ketone 108-10-1 71.93513 08 0
Methyl mercaptan 74-93-1 59.5228 08 0
Methvlene chloride 75-09-2 276.14519 08 0
Perchloroethylene 127-18-4 189.44755 08 0
(tetra chloroethylene)
Propylene dichloride 78-87-5 2.48859 08 0
Tetrachloroethane, 1,1,2,2- 79-34-5 11.25136 08 0
Toluene 108-88-3 2241.32957 08 0
T rich loroethylene 79-01-6 85.68956 08 0
Vinyl chloride 75-01-4 64.45864 08 0
Vinylidene chloride 75-35-4 8.54036 08 0
Xylene 1330-20-7 1685.71159 08 0
8

COPY of RECORD Date Submitted: 6/3/2021 11:57:49
As entered in AERO
Facility Name: Anson County Waste Management Facility Facility ID : 0400052
375 Dozer Drive Permit: 09835
Polkton,NC 28135 County : Anson
DAQ Region : FRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory-Calendar Year 2020
1. Emission Source ID(from permit) IES-2A
or Emission Source Group ID
2. Emission Source Description : Two Diesel fuel above ground storage tanks(12,000 gallon capacity
each)
3. Operating Scenario ID/ OS-2/Municipal solid waste landfill
Description:
4. SCC Number/Description: 50300603/Landfill Dump ; Hazardous: Fugitive Emissions
5. Throughput/units in 2020:
(e.g.production or fuel use):
6. Fuel Information %Sulfur %Ash Heat Content
(If fuel is used)
(Btu/units)
7. Capture Efficiency
(%of Emissions from this Process Vented 75
to Control Device or Stack):
8.Control Device Information
Order CS-ID CD ID Control Device Description
(as listed in permit)
1 CS-1 CD-1 Candle stick type flare(2500 scfm, 75 million Btu per hour heat input
at 506 Btu per cubic foot heat rate of landfill gas
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(Acfni)
Rectangle(L x W)
(in 0.1 feet)
CD-1 VERTICAL 35.11 1 130 53.05 2500 Candlestick flare
STACK
9

Operating Scenario: OS-2 Emission Source/Group ID: IES-2A
10.Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2020)
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 Throughput:
Jan-Feb Dec o March-May ° June-Aug. o Sept.-Nov.
0
2020 25/0 2020 25/0 2020 25/O 2020 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
Pollutants Pollutants Method Code (Net after Factor Control
(Tons/Year) (See Instructions) all controls)
2020
Criteria Emissions- Emission Control
Pollutant Emission Ef
(NAAQS) Criteria Estimation Efficiency
Pollutants Code Pollutants Method Code (Net after Factor Control
(Tons;Year) (See Instructions) all controls)
2020
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
Emissions Emission Control
HAP/TAP CAS Estimation Emission EF
Pollutants(In Alphabetical Order) (see instructions) HAP/TAPS Efficiency Factor Control
(Pounds/Year) Method Code (Net after all controls)
(See Instructions)
2020
10

I
COPY of RECORD Date Submitted: 6/3/2021 11:57:49
As entered in AERO
Facility Name: Anson County Waste Management Facility Facility ID : 0400052
375 Dozer Drive Permit : 09835
Polkton,NC 28135 County : Anson
DAQ Region : FRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory-Calendar Year 2020
1. Emission Source ID(from permit) IES-2A
or Emission Source Group ID
2. Emission Source Description : Two Diesel fuel above ground storage tanks(12,000 gallon capacity
each)
3. Operating Scenario ID/ OS - 5/Fugitive emissions from the diesel tanks
Description:
4. SCC Number/Description: 39999995/Miscellaneous Industrial Processes ; Other Not Classified
5. Throughput/units in 2020: 172942 GAL/yr
(e.g.production or fuel use):
6. Fuel Information %Sulfur %Ash Heat Content
(If fuel is used)
(Btu/units)
7. Capture Efficiency
(%of Emissions from this Process Vented
to Control Device or Stack):
S.Control Device Information :None
Order CS-ID CD ID Control Device Description
(as listed in permit)
9.Emission Release Point(ERP)Information:(Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter##): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
(in 0.1 feet)
IES-4 FUGITIVE(NO 1 72 Area= 1 ASTs
STACK)
11

Operating Scenario: OS- 5 Emission Source/Group ID: IES-2A
10.Operating Schedule:(Source/OperatingSeenario that best characterizes Calendar Year 2020)
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 Throughput:
Jan-Feb+Dec 25% March-May 25% June-Aug. 25% Sept.-Nov. 1 25%
2020 2020 2020 2020
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
Pollutants Pollutants Method Code (Net after Factor Control
(Tons./Year) (See Instructions) all controls)
2020
Criteria Emissions- Emission Control
Pollutant Emission Ef
(NAAQS) Criteria Estimation Efficiency
Pollutants Code Pollutants Method Code (Net after Factor Control
(Tons,'Year) (See Instructions) all controls)
2020
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 0 08
Emissions Emission Control
HAP/TAP CAS Estimation Emission EF
Pollutants(In Alphabetical Order) (see instructions) HAP/TAPS Mthod Code Efficiency Factor Control
e
(Pounds/Year) (Met after all controls)
(See Instructions)
2020
12

COPY of RECORD Date Submitted: 6/3/2021 11:57:49
r As entered in AER O
Facility Name: Anson County Waste Management Facility Facility ID : 0400052
375 Dozer Drive Permit : 09835
Polkton,NC 28135 County : Anson
DAQ Region : FRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory-Calendar Year 2020
1. Emission Source ID(from permit) IES-3B
or Emission Source Group ID
2. Emission Source Description : Gasoline above ground storage tank(1,000 gallon capacity)
3. Operating Scenario ID/ OS- 8/Fugitive Emissions from gasoline tank
Description:
4. SCC Number/Description: 40188898/Fugitive Emissions ; Specify in Comments Field
5. Throughput/units in 2020: 3510 GAL/yr
(e.g.production or fuel use):
6. Fuel Information %Sulfur %Ash Heat Content
(If fuel is used)
(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 permit)
9.Emission Release Point(ERP)Information: (Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter#): \F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
(in 0.1 feet)
IES-4 FUGITIVE(NO 1 72 Area= 1 ASTs
STACK)
13

Operating Scenario: OS- 8 Emission Source/Group ID: IES-3B
p g p
10.Operating Schedule:(Source/OperatingScenario that best characterizes Calendar Year 2020)
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 Throughput:
Jan-Feb+Dec 25% March-May 25% June-Aug. 25% Sept.-Nov. 25%
2020 2020 2020 2020
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
Pollutants Pollutants Method Code (Net after Factor Control
(Tons/Year) (See Instructions) all controls)
2020
Criteria Emissions- Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission Ef
Pollutants Code Pollutants Method Code (Net after Factor Control
(Tonsr'Year) (See Instructions) all controls)
2020
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 0.17 08
Emissions Emission Control
HAP/TAP CAS Estimation Emission EF
Pollutants(In Alphabetical Order) (see instructions) HAP/TAPS Efficiency Factor Control
(Pounds/Year) Method Code (Net after all controls)
(See Instructions)
2020
14

COPY of RECORD Date Submitted: 6/3/2021 11:57:49
As entered in AERO
Facility Name: Anson County Waste Management Facility Facility ID : 0400052
375 Dozer Drive Permit : 09835
Polkton,NC 28135 County : Anson
DAQ Region : FRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory-Calendar Year 2020
1. Emission Source ID(from permit) IES-4A
or Emission Source Group ID
2. Emission Source Description : Two leachate above ground storage tanks(250,000 gallon capacity each)
3. Operating Scenario ID/ OS- 7/Fugitive VOC emissions from leachate tanks.
Description:
4. SCC Number/Description: 40188898/Fugitive Emissions ; Specify in Comments Field
5. Throughput/units in 2020: 5320734 GAL/yr
(e.g.production or fuel use):
6. Fuel Information %Sulfur %Ash Heat Content
(If fuel is used)
(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 permit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
(ERP) ( rY )
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)
IES-4 FUGITIVE(NO 1 72 Area= 1 ASTs
STACK)
15

Operating Scenario: OS-7 Emission Source/Group ID: IES-4A
10.Operating Schedule:(Source/OperatingSeenario that best characterizes Calendar Year 2020)
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 Throughput:
Jan-Feb+Dec 25% March-May 25% June-Aug. 25%_____jSept.-Nov. 25%
2020 2020 2020 2020
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
Pollutants Pollutants Method Code (Net after Factor Control
(Tons/Year) (See Instructions) all controls)
2020
Criteria Pollutant Emissions- Emission Control
Criteria Estimation Emission Ef
(NAAQS) Efficiency
Pollutants Code Pollutants Method Code (Net after Factor Control
(Tons/Pear) (See Instructions) all controls)
2020
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
Emissions Emission Control
HAP/TAP CAS Estimation Emission EF
Pollutants(In Alphabetical order) (see instructions) HAP/TAPS Method Code Efficiency Factor Control
eo oe
(Pounds,'Year) (Net after all controls)
(See Instructions)
2020
Acrylonitrile 107-13-1 0.44402 08
Benzene 71-43-2 0.00002 08
Bromoform 75-25-2 0.44402 08
CFC-
11(Trichlorofluoromethan 75-69-4 0.44402 08
e)
Carbon disulfide 75-15-0 0.44402 08
Carbon tetrachloride 56-23-5 0.00022 08
Chlorobenzene 108-90-7 0.00444 08
Chloroform 67-66-3 0.44402 08
Dichlorobenzene(p), 1,4- 106-46-7 0.02664 08
Dichloropropene, 1,3- 542-75-6 0.44402 08
Ethyl benzene 100-41-4 0.03108 08
Ethyl chloride 75-00-3 0.44402 08
(chloroethane)
Ethylene dibromide 106-93-4 0.00022 1 08
Ethylene dichloride(1,2- 107-06-2 0.00022 08
dichloroethane)
16

Ethylidene dichloride(1,1- 2
dichloroethane) 75-34-3 0.4440� 08
Methyl bromide 74-83-9 0.44402 08
Methyl chloride 74-87-3 0.44402 08
Methyl chloroform 71-55-6 0.00888 08
Methyl ethyl ketone 78-93-3 0.44402 08
Methyl iodide 74-88-4 0.44402 08
Methyl isobutyl ketone 108-10-1 0.44402 08
Methylene chloride 75-09-2 0.00022 08
Perchloroethylene 127-18-4 0.00022 08
(tetrachloroethylene)
Propylene dichloride 78-87-5 0.00022 08
Styrene 100-42-5 0.00444 08
Tetrachloro-2,2-
difluoroethane, 1,1,1,2- 76-11-9 0.44402 08
(CFC 112a)
Tetrachloroethane, 1,1,2,2- 79-34-5 0.44402 08
Toluene 108-88-3 0.0444 08
Trichloroethane, 1,1,2- 79-00-5 0.00022 08
Trichloroethylene 79-01-6 0.00022 08
Vinyl chloride 75-01-4 0.00009 08
Vinylidene chloride 75-35-4 0.44402 08
Xylene 1330-20-7 0.44402 08
17

Facility Total CY 2020 Emissions Summary
COPY of RECORD Date Submitted: 6/3/2021 1.1:57:49
As entered in AERO
Facility Name: Anson County Waste Management Facility Facility ID : 0400052
375 Dozer Drive Permit : 09835
Polkton,NC 28135 County : Anson
DAQ Region : FRO
North Carolina Department of Environmental Quality
Division of Air Quality
Air Pollutant Point Source Emissions Inventory-Calendar Year 2020
Record Facility-Wide Totals From all Permitted and Non-Permitted AirPollutant Emission Sources
Green House Gases Pollutants(GHG
Actual Emissions(Tons/Year)
Pollutant CAS 2020 2019 %Change
Criteria Pollutants
Actual Emissions(Tons/Year)
Pollutant CAS 2020 2019 %Change
CO CO 39.06 29.65 31.736937%
NOx NOx 7.18 5.45 31.743.12%
PM(TSP) TSP 1.77 1.34 32.08955%
PM 10 PM 10 1.77 1.34 32.08955%
PM2.5 PM2.5 1.77 1.34 32.08955%
S02 S02 1.2 .91 31.868134%
VOC VOC 3.76 13.81 -1.3123348%
Hazardous Air Pollutants APS and/or Toxic Air Pollutants APs
Actual Emissions Pounds/Year
Pollutant I CAS 12020 12019 %Change
Pollutant Group:Mercury&Compounds-all total mass,inc Hg Vapor Group Sum:.05609
Mercury,vapor(Component of 7439-97-6 0.05609 .05694 -1.4927986%
lJGC)
Pollutant Group:Total Reduced Sulfur(TRS as total mass)Group Sum:829.09335
Hydrogen sulfide 7783-06-4 769.57056 781.00082 -1.4635372%
Methyl mercaptan 74-93-1 59.5228 60.41473 -1.4763446%
Acrylonitrile 107-13-1 2.27319 2.39718 -5.17233%
Benzene 71-43-2 72.70403 73.79349 -1.4763561%
Bromoform 75-25-2 0.44402 .54061 -17.866856%
CFC-11(Trichlorotluoromethane) 75-69-4 0.44402 .54061 -17.866856%
CFC-12 75-71-8 202.73 737 205.77533 -1.47635%
(D ichlorodifluoromethane)
Carbon disulfide 75-15-0 23.77276 24.21892 -1.8421935%
Carbon tetrachloride 56-23-5 1.03144 1.04695 -1.4814426%
Carbonyl sulfide 463-58-1 10.52675 10.68449 -1.4763511%
Chlorobenzene 108-90-7 24.47227 24.83988 -1.4799223%
18

Chloroform 67-66-3 2.84491 2.97748 -4.452424%
Dichlorobenzene(p), 1,4- 106-46-7 226.2402 229.63575 -1.4786694%'
Dichloropropene, 1,3- 542-75-6 0.44402 .54061 -17.866856%
Ethvl benzene 100-41-4 690.1949 700.54352 -1.4772291%
Ethyl chloride(chloroethane) 75-00-3 15.21052 15.52839 -2.0470257%
Ethyl mercaptan 75-08-1 80.6764 81.88531 -1.4763432%
Ethylene dibromide 106-93-4 8.27628 8.40035 -1.4769530/0
Ethylene dichloride(1,2- 107-06-2 11.37195 11.5424 -1.4767311%
dichloroethane)
Ethylidene dichloride(1,1- 75-34-3 70.67152 71.82045 -1.5997301%
dichloroethane)
Hexane,n- 110-54-3 191.79092 194.66486 -1.4763486%
Hydrogen chloride(hydrochloric 7647-01-0 1236.0194 938.28855 31.731266%
acid)
Methyl bromide 74-83-9 0.44402 .54061 -17.866856%
Methyl chloride 74-87-3 12.48301 12.76 -2.1707675%
Methyl chloroform 71-55-6 21.47152 21.79506 -1.4844637%
Methyl ethyl ketone 78-93-3 729.43384 740.45412 -1.4883115%
Methyl iodide 74-88-4 0.44402 .54061 -17.866856%
Methyl isobutyl ketone 108-10-1 72.37915 73.55367 -1.5968236%
Methylene chloride 75-09-2 276.14542 280.28341 -1.476363%
Perchloroethylene 127-18-4 189.44777 192.28663 -1.4763 726%
(tetrachloroethylene)
Propylene dichloride 78-87-5 2.48881 2.52615 -1.4781357%
Styrene 100-42-5 0.00444 .00541 -17.929766%
Tetrachloro-2.2-difluoroethane, 76-11-9 0.44402 .54061 -17.866856%
1,1,1,2-(CFC 112a)
Tetrachloroethane, 1,1.2.2- 79-34-5 11.69538 11.96056 -2.2171173%
Toluene 108-88-3 2241.3 74 2274.96926 -1.4767327%
Trichloroethane, 1,1,2- 79-00-5 2.2E-4 .00027 -18.518515%
Trichloroethylene 79-01-6 85.68978 86.97386 -1.4763982%0
Vinyl chloride 75-01-4 64.45873 65.42465 -1.4763846%
Vinylidene chloride 75-35-4 8.98438 9.20895 -2.438609%
Xylene 1330-20-7 1686.1556 1711.51206 -1.481523%
19

COPY of RECORD Date Submitted: 6/3/2021 11:57:49
As entered in AERO
Facility Name: Anson County Waste Management Facility Facility ID : 0400052
375 Dozer Drive Permit : 09835
Polkton,NC 28135 County : Anson
DAQ Region : FRO
Comments From Facility:
i
20

ATTACHMENT B
RY2020 EMISSIONS INVENTORY SUPPORTING CALCULATIONS

ANSON COUNTY WASTE MANAGEMENT FACILITY 2020 EMISSIONS
x NO, sox sox CO CO PM1, " VOCs VOCs RAPS IIAI's
(Ibs/hr) (tpy) (lbs/hr) (tpy) (Ibs/hr) (tpy) (Ibs/hr) (tpy) (Ibs/hr) (tpy) (Ibs/hr) (tpy)
LFG Candlestick Flare 1.64 7,19 027 120 8.92 39.06 0.40 1.77 0.02 0.09 0.16 0.71
(CD-1)
Landfill Fugitive Emissions
0.80 3.50 0.88 3.84
ES-1
Total ES-1 Emissions 1.64 7.18 0.27 1_'0 8.92 39.06 0.40 1.77 0.82 3.59 1.04 4.55
Leachate ASTs 0.0008 0.0034 0.0008 0.0034
Other ASTs 0.0392 0.1718 0.0392 0.1718
Total AST Emissions 0.0400 0.1752 0.0400 0.1752
GRAND TOTAL EMISSIONS 1.64 7.18 0.27 1.20 8.92 39.06 0.40 1.77 0.86 3.76 1.08 4.72

WASTE INDUSTRY AIR COALIATION CONCENTRATIONS FOR LFG CONSTITUENTS
ES-1 Total LFG Emissions(Fugitive LFG and Candlestick Flare Emissions)
Default
Concentration Emissions Emissions Emissions Emissions
Compound Molecular Weight (ppmv) (lbs/hr) (lbs/day) (lbs/yr) (tons/yr)
1,1,1-Trichloroethane
(methyl chloroform)1'4 133.41 0.168 0.0025 0.0590 211.46264 0.0107
1,1,2,2-Tetrachloroethane' 167.85 0.070 0.0013 0.0309 11.25136 0.0056
1,1-Dichloroethane
(ethylidene dichloride)' 98.97 0.741 0.0080 0.1930 70.22750 0.0351
1,1-Dichloroethee
(vinylidene chloride)' 96.94 0.092 0.0010 0.0235 8.54036 0.0043
1,2-Dichloroethane
(ethylene dichloride)' 9896 0.120 0.0013 0.0312 11.37173 ' 0.0057
1,2-Dichloropropane
(propylene dichloride)' 112.99 0.023 0.0003 0.0068 2.48859 VO.0012
Acrylonitrile' 53.06 0.036 0.0002 0.0050 1.82917 0.0009
Carbon disulfide) 76.13 0.320 0.0027 0.0641 23.32874 0.0117
Carbon tetrachloride' 153.84 0.007 0.0001 0.0028 1.03122 0.0005
Carbonyl sulfide' 60.07 0.183 0.0012 0.0289 10.52675 0.0053
Chlorobenzene' 112.56 0.227 0.0028 0.0672 24.46783` 0.0122
Chloroethane
(ethyl chloride)' 64.52 0.239 0.0017 0.0406 14.76650 0.0074
Chloroform' 119.39 0.021 0.0003 0.0066 2.40089 0.0012
Chloromethane
(Methyl Chloride) 50.49 0.249 0.0014 0.0331 12.03899 0.0060
Dichlorobenzene2 147.00 1.607 0.0259 0.6216 226.21357 A 0.1131
Dichlorodifluoromethane4 120.91 1.751 0.0232 0.5571 202.73737 0.1014
Dichloromethane
(methylene chloride)I,4 84.94 3.395 0.0316 0.7588 1 76.14519 0.1381
Hazardous Air Pollutants listed in Title III of the 1990 Clean Air Act Amendments.
2Source tests did not indicate whether this compound was the para-or ortho-isomer.
The para isomer is a Title III-listed HAP.
3No data were available to speciate total Hg into the elemental and organic forms.
4Non-Volatile Organic Compounds(Non-VOCs)as indicated in 40 CFR 51.100.
'In accordance with the assumption found in AP-42-13.5.2,a 98%destruction efficiency is assumed.
Page 1

WASTE INDUSTRY AIR COALIATION CONCENTRATIONS FOR LFG CONSTITUENTS
ES-1 Total LFG Emissions(Fugitive LFG and Candlestick Flare Emissions)
Delault
Concentration Emissions Emissions Emissions Emissions
Compound Molecular Weight (ppmv) (lbs/hr) (lbs/day) (lbs/yr) (tons/yr)
Ethyl mercaptan(ethanethiol) 62.13 1.356 0.0092 0.2217 80.67640 0.0403
Ethylbenzene' 106.16 6.789 0.0790 1.8964 690.16379 0.3451
Ethylene dibromide 187.88 0.046 0.0009 0.0227 8.27606 Z74 0.0041
Hexane' 86.18 2.324 0.0220 0.5270 191.79093 0.0959
Hydrochloric Acid 36.46 42.000 0.1590 3.8153 1,236.01935' 0.6180
Hydrogen sulfide 34.08 23.578 0.0881 2.1143 769.47055 0.3847
Mercury(total)',3 200.61 2.92E-04 6.42E-06 0.0002 0.05609 2.80E-05
Methyl ethyl ketone 72.11 10.557 0.0835 2.0030 728.98983 0.3645
Methyl isobutyl ketone' 100.16 0.750 0.0082 0.1977 71.93513 0.0360
Methyl mercaptan 48.11 1.292 0.0068 0.1636 59.52280 0.0298
Perchloroethylene
(tetrachloroethylene)''4 165.83 1.193 0.0217 0.5205 189.44755 0.0947
Trichloroethylene
(trichloroethene)' 131.40 0.681 0.0098 0.2354 85.68956 0.0428
Vinyl chloride 62.50 1.077 0.0074 0.1771 64.45864 1, 0.0322
Xylenes' 106.16 16.582 0.1930 4.6318 1,685.71159 0.8429
Benzene' 78.11 0.972 0.0083 0.1998 72.70401 0.0364
Toluene' 92.13 25.405 0.2566 6.1585 2,241.32957 1.1207
'Hazardous Air Pollutants listed in Title III of the 1990 Clean Air Act Amendments.
2Source tests did not indicate whether this compound was the para-or ortho-isomer.
The para isomer is a Title III-listed HAP.
3No data were available to speciate total Hg into the elemental and organic forms.
4Non-Volatile Organic Compounds(Non-VOCs)as indicated in 40 CFR 51.100.
5In accordance with the assumption found in AP-42-13.5.2,a 98%destruction efficiency is assumed.
Page 2

WASTE INDUSTRY AIR COALIATION CONCENTRATIONS FOR LFG CONSTITUENTS
ES-1 Total LFG Emissions(Fugitive LFG and Candlestick Flare Emissions)
I
Total VOCs 0.82 lbs/hour
Total VOCs 3.59 tons/yr
Total HAPs 4.55 tons/yr
PMIo Emissions 0.46 lbs/hr
PMIo Emissions 1.77 tons/yr
CO Factor
(Manufacturer Specifications) 0.31 lbs/MviBTU
CO Emissions 10.05 lbs/hr
CO Emissions 39.06 ton/yr
NO,Factor
(Manufacturer Specifications) 0.068 lbs/M1v1BTU
NO,Emissions 1.85 lbs/hr
NQ,Emissions 7.18 tons/yr
I
Page 3

WASTE INDUSTRY AIR COALIATION CONCENTRATIONS FOR LFG CONSTITUENTS
ES-1 Total LFG Emissions(Fugitive LFG and Candlestick Flare Emissions)
Sulfur Molecular Weight= 32.066 g/gmole
Sulfur Concentration=
(AP-42-2.4.4.2) 46.9 ppmv
CH4 generation rate= 5,908,021 m3/year
Standard Pressure= 1 atm
Universal Gas Constant= 8.21E-05 m3-atm/gmol-°K
Standard Temperature= 298.00 °K
Multiplication Factor=
(50%CH4) 2.0020 unitless
Sulfur Emission Rate=
(AP-42-2.4.4.1 Eq.3) 555 m3/year
Total Uncontrolled Mass
Emissions of S02_
(AP-42-2.4.4.1 Eq.4) 727 kg/year
Tota Controlled Mass
Emissions of S02=
(AP-42-42-2.4.4.1 Eq.7) 1,091 kg/N car
'Lotal Controlled ,
Emissions= 2,405 Ibs/Near
Total Controlled S02
Emissions= 1.20 tons/year
HCl Molecular Weight= 36.461 g/gmole
HCl Concentration=
(AP-42-2.4.4.2) 42.0 ppmv
CH4 generation rate= 5,908,021 m3/year
Standard Pressure= 1 atm
Universal Gas Constant= 8.21E-05 m3-atm/gmol-°K
Standard Temperature= 298.00 °K
Multiplication Factor=
(50%C114) 2.0020 unitless
Chlorine Emission Rate=
(AP-42-2.4.4.1 Eq.3) 497 m3/year
Uncontrolled Mass Emissions
of Chlorine= (AP-42-
2.4.4.1 Eq.4) 741 kg/year
Total Chlorine Controlled
Emissions=
(AP-42-2.4.4.1 Eq. 10) -560.81 kg/year
'l'otal Chlorine Controllecl
Emissions= 0.62 tons/year
ota orine Contro=e
Emissions= 0.16 Ibs/hr
Page 4

TOAL LEACHATE TANK EMISSION SUMMARY
Annual Annual
Sample Emissions Emissions Annual Emissions
Compound Concentration` Units (lbs/hr) (lbs/year) (tons/yr)
1,1,1-Trichloroethane
(methyl chloroform)1,4,6 0.200 µg/L 1.0137E-06 8.8803E-03 4.4402E-06
1,1,1,2-Tetrachloroethane 1,5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
1,1,2,2-Tetrachloroethane"5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
1,1-Dichloroethane
(ethylidene dichloride)''' 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
1,1,2 Trichloroethanel'6 0.005 µg/L 2.5343E-08 2.2201E-04 1.1100E-07
1,2 Dichlorobenzene5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
1,1-Dichloroethene
(vinylidene chloride)"' 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
1,2-Dichloroethane
(ethylene dichloride)1'6 0.005 µg/L 2.5343E-08 2.2201E-04 1.1100E-07
1,2-Dichloropropane(propylene
dichloride)1'6 0.005 µg/L 2.5343E-08 2.2201E-04 1.1100E-07
1,2-Dibromo-3-chloropropane6 0.000 µg/L 1.0137E-09 8.8803E-06 4.4402E-09
1,2 Dibromoethanel'6 0.005 µg/L 2.5343E-08 2.2201E-04 1.1100E-07
1,4 Dichlorobenzenel'6 0.600 µg/L 3.0412E-06 2.6641E-02 1.3320E-05
Acetones 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Acrylonitrile" 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Bromochloromethane5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Bromodichloromethane5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Bromoforml'S 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Bromomethanel's 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Carbon disulfide1,5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Carbon tetrachloridel'6 0.005 µg/L 2.5343E-08 2.2201E-04 1.1100E-07
Chlorobenzenel'6 0.100 µg/L 5.0687E-07 4.4402E-03 2.2201E-06
Chloroethane
(ethyl chloride)''' 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Chloroform1,5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Chloromethane5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Dibromochloromethane5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Dibromomethane5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
cis-1,2-Dichloroethene 5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
cis-1,3 Dichloropropene5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
trans-1,3 Dichloropropene5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
trans-l,4-Dichloro-2-butene5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Dichloromethane
(methylene chloride)1,4,6 0.005 µg/L 2.5343E-08 2.2201E-04 1.1100E-07
Ethylbenzenel'6 0.700 µg/L 3.5481E-06 3.1081E-02 1.5541E-05
Iodomethane5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
MEK5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
MBK5 10.000 1g/L 5.0687E-05 4.4402E-01 2.2201E-04
MIK5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04

TOAL LEACHATE TANK EMISSION SUMMARY
Annual Annual
Sample Emissions Emissions Annual Emissions
Compound Concentrations Units (Ibs/hr) (Ibs/year) (tons/yr)
Perchloroethylene
(tetrachloroethylene)''4,6 0.005 µg/L 2.5343E-08 2.2201E-04 1.1100E-07
Styrene''6 0.100 µg/L 5.0687E-07 4.4402E-03 2.2201E-06
t-1,2-dichloroethene' 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Fluorotrichloromethane5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Trichloroethylene
(trichloroethene)''6 0.005 µg/L 2.5343E-08 2.2201E-04 1.1100E-07
Vinyl acetate 0.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
Vinyl chloride''6 0.002 µg/L 1.0137E-08 8.8803E-05 4.4402E-08
Xylenes''6 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Benzene''6 0.001 µg/L 2.5343E-09 2.2201E-05 1.1100E-08
Toluene"" 1.000 4.19/1- 1 5.0687E-06 4.4402E-02 2.2201E-05
Hazardous Air Pollutants listed in Title III of the 1990 Clean Air Act Amendments
2Source tests did not indicate whether this compound was the para-or ortho-isomer.
The para isomer is a Title III-listed HAP.
3No data were available to speciate total Hg into the elemental and organic forms.
4Non-Volatile Organic Compounds(Non-VOCs)as indicated in 40 CFR 5 1.100
5 Compounds that are not in the National Priority Drinking Water Regulations MCL list. Because leachate is a
liquid,conservative assumption concentrations of 10 µg/L have been utilized.
6 Compounds are listed as both a HAP and are on the National Priority Drinking Water Regulations MCL list.
A conservative leachate sample concentration estimate of 1000 times the MCL(µg/L)has been used to estimate
emissions through volitization and evaporation.
Total VOCs
HAPs 0.003 tons/yr
Total VOCs
Non-Haps 0.003 tons/yr
Total Non-VOCs
HAPs 0.000 tons/yr
Total Non-VOCs
Non-Haps 0.000 tons/yr

WASTE INDUSTRY AIR COALIATION CONCENTRATIONS FOR LFG CONSTITUENTS
CD-1 LFG CANDLESTICK FLARE
2500 SCFM CANDLESTICK FLARE
Default
Concentration Emissions Emissions
Compound Molecular Weight (ppmv) (lbs/hr) (tons/yr)
1,1,1-Trichloroethane,
(methyl chloroform)''4 133.41 0.168 6.3395E-05 2.4645E-04
1,1,2,2-Tetrachloroethane' 167.85 0.070 3.3233E-05 1.2920E-04
1,1-Dichloroethane
(ethylidene dichloride)' 98.97 0.741 2.0743E-04 8.0641E-04
1,1-Dichloroethee
(vinylidene chloride)' 96.94 0.092 2.5226E-05 9.8067E-05
1,2-Dichloroethane
(ethylene dichloride)' 98.96 0.120 3.3589E-05 1.3058E-04
1,2-Dichloropropane
(propylene dichloride)' 112.99 0.023 7.3506E-06 2.8576E-05
Acrylonitrile' 53.06 0.036 5.4029E-06 2.1004E-05
Carbon disulfide' 76.13 0.320 6.8907E-05 2.6788E-04
Carbon tetrachloride' 153.84 0.007 3.0460E-06 1.1841E-05
Carbonyl sulfide' 60.07 0.183 3.1093E-05 1.2088E-04
Chlorobenzene' 112.56 0.227 7.2271E-05 2.8096E-04
Chloroethane
(ethyl chloride)' 64.52 0.239 4.3616E-05 1.6956E-04
Chloroform' 119.39 0.021 7.0916E-06 2.7569E-05
Chloromethane 50.49 0.249 3.5560E-05 1.3824E-04
Dichlorobenzene2 147.00 1.607 6.6817E-04 2.5976E-03
Dichlorodifluoromethane4 120.91 1.751 5.9883E-04 2.3280E-03
Dichloromethane
(methylene chloride)''4 84.94 3.395 8.1566E-04 3.1709E-03
Hazardous Air Pollutants listed in Title III of the 1990 Clean Air Act Amendments.
2Source tests did not indicate whether this compound was the para-or ortho-isomer.
The para isomer is a Title III-listed HAP.
No data were available to speciate total Hg into the elemental and organic forms.
Non-Volatile Organic Compounds(Non-VOCs)as indicated in 40 CFR 51.100.
In accordance with the assumption found in AP-42-13.5.2,a 98%destruction efficiency is assumed.
Page 1

WASTE INDUSTRY AIR COALIATION CONCENTRATIONS FOR LFG CONSTITUENTS
CD-1 LFG CANDLESTICK FLARE
2500 SCFM CANDLESTICK FLARE
Default
Concentration Emissions Emissions
Compound Molecular Weight (ppmv) (lbs/hr) (tons/yr)
Ethyl mercaptan(ethanethiol) 62.13 1.356 2.3830E-04 9.2639E-04
Ethylbenzene' 106.16 6.789 2.0386E-03 7.9250E-03
Ethylene dibromide 187.88 0.046 2.4445E-05 9.5033E-05
Hexane' 86.18 2.324 5.6650E-04 2.2023E-03
Hydrochloric Acid 36.46 42.000 0.1590 0.6180
Hydrogen sulfide 34.08 23.578 2.27E-03 8.84E-03
Mercury(total)"' 200.61 2.920E-04 1.66E-07 6.44E-07
Methyl ethyl ketone' 72.11 10.557 2.15E-03 8.37E-03
Methyl isobutyl ketone' 100.16 0.750 2.12E-04 8.26E-04
Methyl mercaptan 48.11 1.292 1.76E-04 6.83E-04
Perchloroethylene
(tetrachloroethylene)''4 165.83 1.193 5.60E-04 2.18E-03
Trichloroethylene
(trichloroethene)' 131.40 0.681 2.53E-04 9.84E-04
Vinyl chloride 62.50 1.077 1.90E-04 7.40E-04
Xylenes' 106.16 16.582 4.98E-03 1.94E-02
Benzene' 78.11 0.972 2.15E-04 8.35E-04
Toluene' 92.13 25.405 6.62E-03 2.57E-02
1 Hazardous Air Pollutants listed in Title III of the 1990 Clean Air Act Amendments.
2Source tests did not indicate whether this compound was the para-or ortho-isomer.
The para isomer is a Title III-listed HAP.
3No data were available to speciate total Hg into the elemental and organic forms.
Non-Volatile Organic Compounds(Non-VOCs)as indicated in 40 CFR 51.100.
5In accordance with the assumption found in AP-42-13.5.2,a 98%destruction efficiency is assumed.
Page 2

WASTE INDUSTRY AIR COALIATION CONCENTRATIONS FOR LFG CONSTITUENTS
CD-1 LFG CANDLESTICK FLARE
2500 SCFM CANDLESTICK FLARE
2020 LFG Combustion Rate 894 scfm
417,279,580 scf/year
7,775 hours/year
Molar Flow rate 141.42 lbmole LFG/hr
Total VOCs 0.02 lbs/hour
Total VOCs 0.08 tons/yr
Total HAPs 0.71 tons/yr
PM10 Emissions 0.46 lbs/hr
PM10 Emissions 1.77 tons/yr
CO Factor
(Manufacturer Specifications) 0.37 lbs/MvIBTU
CO Emissions 10.05 lbs/hr
CO Emissions 39.06 ton/yr ✓
NO,,Factor
(Manufacturer Specifications) 0.068 lbs/MMBTU
NO,,Emissions 1.85 lbs/hr /
NO,.Emissions 7.18 tons/yr ✓
Page 3
I

WASTE INDUSTRY AIR COALIATION CONCENTRATIONS FOR LFG CONSTITUENTS
CD-1 LFG CANDLESTICK FLARE
2500 SCFM CANDLESTICK FLARE
Sulfur Molecular Weight= 32.066 g/gmole
Sulfur Concentration=
(AP-42-2.4.4.2) 46.9 ppmv
CH4 generation rate= 5,908,021 MI/year
Standard Pressure= 1 atm
Universal Gas Constant= 8.21 E-05 m3-atm/gmol-°K
Standard Temperature= 298.00 °K
Multiplication Factor=
(50%CH4) 2.0020 unitless
Sulfur Emission Rate=
(AP-42-2.4.4.1 Eq.3) 555 m3/year
Total Uncontrolled Mass
Emissions of S02=
(AP-42-2.4.4.1 Eq.4) 727 ka/near
Total Controlled Mass
Emissions of S02=
(AP-42-42-2.4.4.1 Eq.7) 1,091 kg/year
Total Controlled S02
Emissions= 1.20 tons/year
HCl Molecular Weight= 36.461 g/gmole
HCl Concentration=
(AP-42-2.4.4.2) 42.0 ppmv
CH4 generation rate= 5,908,021 m3/yeas
Standard Pressure= 1 atm
Universal Gas Constant= 8.21E-05 m3-atm/gmol-°K
Standard Temperature= 298.00 °K
Multiplication Factor=
(50%CH4) 2.0020 unitless
Chlorine Emission Rate=
(AP-42-2.4.4.1 Eq.3) 497 m3/year
Uncontrolled Mass Emissions
of Chlorine= (AP-42-
2.4.4.1 Eq.4) 741 kg/year
Total Chlorine Controlled
Emissions=
(AP-42-2.4.4.1 Eq.10) 560.81 kg/year
Total Chlorine Controlled
Emissions= 0.62 tons/year
ota orme Control e
Emissions= 0.16 lbs/hr
Page 4

CD-1 LFG CANDLESTICK FLARE EMISSION EXAMPLE CALCULATIONS
Molar Flow Rate= 565 ft X 60 min X 1 ATM - .73024 atmft3/lbmole OR X 519.67 OR = 89.33 lbmole
min hr hr
CH4 Generation ft3 m3 min o/o _ m3
565 X 0.028316847 , 525,600 X 0.5 CH4 - 4,204,542
Rate= mui ft yr yr
VOC/HAPs 0.239 ppmv X 64.52 MW X 89 33 IbmoleLFG X U 02 Destruct = 0.0000 lbs
Emissions= 1.00E+06 hr Efficiency hr
ft3 17 lbs lb/hr o _ lbs
PM1e Emissions= 565 X - 16,700 X 0.5 CH4 - 0.29
min 1,1,000,000 dscf dscfm /o hr
AP-42 Table 2.4-5'
ft3 BTU CH4 min Ibs lbs
CO Emissions= 565 X 1012 X 60 X 0.31 X 0.5 CH4 - 1,000,000 = 5.32
min ft3 a hr mmbal hr
ft3 BTU CH4 min lbs lbs
NO,Emissions= 565 \ 1012 X 60 X 0,068 X 0.5 CH4 - 1,000,000 = 1.17
min ft 3 hr mmbtu hr
SO Emissions Multi m3 m3
2 2.UO2 X 5,908,021 ?� 46.9 ppmv - 1,000,000 = 554.73
Rate= Factor yr yr
(AP42-2.4.4.1 Eq.3)
Uncontrolled Mass S55 m 3 X 32.066 g X 1 ATM _ 8.21E-05 M3-atm X 1000 g kg
X 298.00 = 727.49
Emission Rate= yr mole g/mole-°K kg yr
(AP-42-2.4.4.1 Eq.4)
Controlled Mass �_ kg
727.49 X 0.75 X 2 MW Ratio SOZ = 1,091.24
Emission Rate= yr yr
(AP-42-42-2.4.4.1 Eq.7)
02 Emissions m3 3
2.002 Multi X 5,908,021 X 42 ppmv _ 1,000,000 496.77 m
Rate= Factor yr yr
(AP42-2.4.4.1 Eq.3)
Cl2 Uncontrolled Mass 497 m' X 36.461 X 1 ATM - 8.21E-05 M3-atm X 1000 g X 298.00 = 740.78 -�
Emission Rate= yr mole g/mole-°K kg yr
(AP-42-2.4.4.1 Eq.4)
Total 02 Emissions= 740.78 kg Control Device kg
(AP-42-2.4.4.1 Eq.10) yr X 0.75 X 1.03 MW Ratio CLZ X 0.98 560.81
Efficiency =
Page 1

0
WASTE INDUSTRY AIR COALIATION CONCENTRATIONS FOR LFG CONSTITUENTS
ES-1 FUGITIVE LFG EMISSIONS
Default
Concentration Emissions Emissions
Compound Molecular Weight (ppmv) (lbs/hr) (tons/yr)
1,1,1-Trichloroethane
(methyl chloroform)1'4 133.41 0.168 0.0024 0.0105
1,1,2,2-Tetrachloroethane' 167.85 0.070 0.0013 0.0055
1,1-Dichloroethane
(ethylidene dichloride)1 98.97 0.741 0.0078 0.0343
1,1-Dichloroethee
(vinylidene chloride)1 96.94 0.092 0.0010 0.0042
1,2-Dichloroethane
(ethylene dichloride)1 98.96 0.120 0.0013 0.0056
1,2-Dichloropropane
(propylene dichloride)' 112.99 0.023 0.0003 0.0012
Acrylonitrilel 53.06 0.036 0.0002 0.0009
Carbon disulfide) 76.13 0.320 0.0026 0.0114
Carbon tetrachloride' 153.84 0.007 0.0001 0.0005
Carbonyl sulfide' 60.07 0.183 0.0012 0.0051
Chlorobenzenel 112.56 0.227 0.0027 0.0120
Chloroethane
(ethyl chloride)' 64.52 0.239 0.0016 0.0072
Chloroform' 119.39 0.021 0.0003 0.0012
Chloromethane 50.49 0.249 0.0013 0.0059
[! Dichlorobenzene2 147.00 1.607 0.0252 0.1105)
imchlorodifluoromethane4 120.91 1.7�1 0.0226 0.0990
Dichloromethane
ethylene chloride)''4 84.94 3.395 0.0308 0.1349
1 Hazardous Air Pollutants listed in Title III of the 1990 Clean Air Act Amendments.
2Source tests did not indicate whether this compound was the para-or ortho-isomer.
The para isomer is a Title III-listed HAP.
3No data were available to speciate total Hg into the elemental and organic forms.
Non-Volatile Organic Compounds(Non-VOCs)as indicated in 40 CFR 51.100.
Page 1

0
WASTE INDUSTRY AIR COALIATION CONCENTRATIONS FOR LFG CONSTITUENTS
ES-1 FUGITIVE LFG EMISSIONS
Default
Concentration Emissions Emissions
Compound Molecular Weight (ppmv) (lbs/hr) (tons/yr)
Ethyl mercaptan(ethanethiol) 62.13 1.356 0.0090 0.0394
Ethylbenzene' 106.16 6.789 0.0770 0.3372
Ethylene dibromide 187.88 0.046 0.0009 0.0040
Hexane' 86.18 2.324 0.0214 0.0937
Hydrogen sulfide 34.08 23.578 0.0858 0.3759
Mercury(total)''3 200.61 2.92E-04 0.0000 2.74E-05
Methyl ethyl ketone 72.11 10.557 0.0813 0.3561
Methyl isobutyl ketone' 100.16 0.750 0.0080 0.0351
Methyl mercaptan 48.11 1.292 0.0066 0.0291
Perchloroethylene
(tetrachloroethylene)''4 165.83 1.193 0.0211 0.0925
Trichloroethylene
(trichloroethene)' 131.40 0.681 0.0096 0.0419
Vinyl chloride' 62.50 1.077 0.0072 0.0315
Xylenes 106.16 16.582 0.1880 0.8235
Benzene 78.11 0.972 1 0.0081 0.0355
Toluene' 92.13 25.405 0.2500 1.0949
Hazardous Air Pollutants listed in Title III of the 1990 Clean Air Act Amendments.
2Source tests did not indicate whether this compound was the para-or ortho-isomer.
The para isomer is a Title III-listed HAP.
3No data were available to speciate total Hg into the elemental and organic forms.
Non-Volatile Organic Compounds(Non-VOCs)as indicated in 40 CFR 51.100.
LFG Generation Rate
(LandGEM Ver 3.02) 1,469 scfin
LFG Generation Rate
(LandGEM Ver 3.02) 772,328,794 scf/yr
Calculated Collection
Efficiency 54.0%
Molar Flow rate 232.33 lbmole LFG/hr
Total VOCs 0.80 lbs/hour
Total VOCs 3.50 tons/yr
Total HAPs 3.84 tons/yr
Page 2

i
ES-1 LFG FUGITIVE EMISSION EXAMPLE CALCULATIONS
Molar Flow Rate= 1469 ft; X 60 min X 1 ATM - 73024 atmft;/lbmole°R X 519.67"R = 232.33 Ibmole
min hr hr
Chlorobenzene 0.227 ppmv X 112.56 MW X 232.33 IbmoleLFG K 0.460 Collection — 0.0027 lbs
Emissions= 1.00E+06 hr Efficiency hr
ICI
I
Page 1

Summary Report
Landfill Name or Identifier: Anson County Waste Management Facility
Date: Thursday, June 3, 2021
Description/Comments:
LFG Generation Estimate for RY2020.
About LandGEM:
ra 1
First-Order Decomposition Rate Equation: = kL0la —kti j
a=1 j=0.1 1
Where,
OcH4=annual methane generation in the year of the calculation(m 3/year)
i=1-year time increment M;=mass of waste accepted in the ith year(Mg)
n=(year of the calculation)-(initial year of waste acceptance) t;j=age of the jth section of waste mass M;accepted in the ith year
j=0.1-year time increment (decimal years,e.g.,3.2 years)
k=methane generation rate(year-)
Lo=potential methane generation capacity(m 3/Mg)
LandGEM is based on a first-order decomposition rate equation for quantifying emissions from the decomposition of landfilled waste in municipal
solid waste(MSW)landfills.The software provides a relatively simple approach to estimating landfill gas emissions.Model defaults are based on
empirical data from U.S.landfills.Field test data can also be used in place of model defaults when available.Further guidance on EPA test
methods,Clean Air Act(CAA)regulations,and other guidance regarding landfill gas emissions and control technology requirements can be found
at http://www.epa.gov/ttnatwOl/landfill/landflpg.html.
LandGEM is considered a screening tool—the better the input data,the better the estimates.Often,there are limitations with the available data
regarding waste quantity and composition,variation in design and operating practices over time,and changes occurring over time that impact the
emissions potential.Changes to landfill operation,such as operating under wet conditions through leachate recirculation or other liquid additions,
will result in generating more gas at a faster rate.Defaults for estimating emissions for this type of operation are being developed to include in
LandGEM along with defaults for convential landfills(no leachate or liquid additions)for developing emission inventories and determining CAA
applicability.Refer to the Web site identified above for future updates.
Input Review
LANDFILL CHARACTERISTICS
Landfill Open Year 2001
Landfill Closure Year(with 80-year limit) 2031
Actual Closure Year(without limit) 2031
Have Model Calculate Closure Year? Yes
Waste Design Capacity 16,216,751 short tons
MODEL PARAMETERS
Methane Generation Rate,k 0.020 year-'
Potential Methane Generation Capacity,Lo 100 m 3/Mg
NMOC Concentration 4,000 ppmv as hexane
Methane Content 50 %by volume
GASES/POLLUTANTS SELECTED
Gas/Pollutant#1: Total landfill gas
Gas/Pollutant#2: Methane
Gas/Pollutant#3: Carbon dioxide
Gas/Pollutant#4: NMOC

Summary Report
Landfill Name or Identifier: Anson County Waste Management Facility
Date: Thursday, June 3, 2021
Description/Comments:
LFG Generation Estimate for RY2020.
waste ACceptea Waste-in-Place Generation
Year (short tons/yr) (short tons) (avg.scfm)
2001 236,580 0 0
2002 236,580 236,580 57
2003 236,580 473,160 113
2004 236,580 709,740 168
2005 236,580 946,320 222
2006 113,173 1,182,900 275
2007 258,288 1,296,073 297
2008 155,225 1,554,361 354
2009 196,004 1,709,586 384
2010 269,790 1,905,590 424
2011 297,549 2,175,380 481
2012 243,967 2,472,929 544
2013 372,201 2,716,896 592
2014 496,950 3,089,097 670
2015 454,706 3,586,047 778
2016 534,408 4,040,753 872
2017 713,953 4,575,161 984
2018 731,504 5,289,114 1,138
2019 836,873 6,020,618 1,292
2020 814,909 6,857,491 1,469
2021 814,909 7,672,400 1,638
2022 814,909 8,487,309 1,803
2023 814,909 9,302,218 1,964
2024 814,909 10,117,127 2,123
2025 814,909 10,932,036 2,278
2026 814,909 11,746,945 2,430
2027 814,909 12,561,854 2,579
2028 814,909 13,376,763 2,726
2029 814,909 14,191,673 2,869
2030 814,909 15,006,582 3,009
2031 395,260 15,821,491 3,147
2032 0 16,216,751 3,181
2033 0 16,216,751 3,118
2034 0 16,216,751 3,056
L
5 0 16,216,751 2,995
6 0 16,216,751 2,936
7 0 16,216,751 2,878
8 0 16,216,751 2,821
9 0 16,216,751 2,765
0 0 16,216,751 2,710

SUMMARY OF INSIGNIFICANT ACTIVITIES
Description Emission Point as VOCHAP Emissions
Referenced in Title V Application (lbs/hr) HAP Emissions(tpy)
12,000 Gallon AST1 0.0000E+00 0.0000E+00
12,000 Gallon AST1 6.8607E-04 3.0050E-03
250,000 Gallon AST2 0.0000E+00 0.0000E+00
380,000 Gallon AST2 7.7263E-04 3.3841E-03
500 Gallon AST1 3.8531E-02 1.6877E-01
Total WUHAN 3.9990E-02 1.7515E-01
Note: 1. VOC/HAP emissions calculated using EPAs Tank 4.01d Program
2. Leachate tank emissions were calculated with the assumption of 100%volatility.Therefore,the emissions
associated with these tanks are more conservative than the output that would be produced by Tanks 4.01 d
3. AP-42 Table 3.3-1 Does not identify any HAPs for gasoline engines
Page 1

LEACHATE TANK EMISSION SUMMARY
250,000 Gallon
Emissions from the leachate tanks were estimated based on comparison of National Priority Drinking Water
(MCL)concentrations of each pollutant. It has been assumed that all VOCs and TAPs in the leachate tank
influent evaporate.The average emissions(lbs/hr)were calculated by multiplying the concentration of each
pollutant by the estimated influent rate of leachate.
The estimated influent rate used of
0.00 gpd 0 M
Summary of Emissions are below:
Emission assumptions
Estimated total tank throughput gal/min 0.00 Units Rg
Estimated total tank throughput gal/day 0.00
Tank pera on days/year 365
Annual Annual
Emissions Emissions Annual Emissions
Compound Sample Concentrations Units (lbs/hr) (lbs/year) (tons/yr)
1,1,1-Trichloroethane
(methyl chloroform)1'4'6 0.200 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
1,1,1,2-Tetrachloroethane''S 10.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
1,1,2,2-Tetrachloroethane''5 10.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
1,1-Dichloroethane
(ethylidene dichloride)''5 10.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
1,1,2 Trichloroethane''6 0.005 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
1,2 Dichlorobenzene5 10.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
1,1-Dichloroethene
(vinylidene chloride)' 10.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
1,2-Dichloroethane
(ethylene dichloride)''6 0.005 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
1,2-Dichloropropane(propylene
dichloride)1'6 0.005 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
1,2-Dibromo-3-chloropropaneb 0.000 lLg/L 0.0000E+00 0.0000E+00 0.0000E+00
1,2 Dibromoethane''6 0.005 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
1,4 Dichlorobenzene''6 0.600 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
Acetones 10.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
Acrylonitrile"' 10.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
Bromochloromethane5 10.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
Bromodichloromethane5 10.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
Bromoform''5 10.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
Bromomethane"5 10.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
Carbon disulfide"5 10.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
Carbon tetrachloride''6 0.005 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
Chlorobenzene''6 0.100 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
Chloroethane
(ethyl chloride)''' 10.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
Chloroform''' 10.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
Chloromethane5 10.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
Dibromochloromethane5 10.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
Dibromomethane5 10.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
cis-1,2-Dichloroethene' 10.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
cis-1,3 Dichloropropene5 10.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
trans-1,3 Dichloropropene' 10.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
trans-1,4-Dichloro-2-butene5 10.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
Dichloromethane
(methylene chloride)''4,6 0.005 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
Ethylbenzene',6 0.700 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
Iodomethane5 10.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
MEW 10.000 4g/L 0.0000E+00 0.0000E+00 0.0000E+00
MBK' 10.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
MIK' 10.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
Perchloroethylene
(tetrachloroethylene)''4,6 0.005 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
Page 1

LEACHATE TANK EMISSION SUMMARY
250,000 Gallon
Emissions from the leachate tanks were estimated based on comparison of National Priority Drinking Water
(MCL)concentrations of each pollutant. It has been assumed that all VOCs and TAPS in the leachate tank
influent evaporate.The average emissions(lbs/hr)were calculated by multiplying the concentration of each
pollutant by the estimated influent rate of leachate.
The estimated influent rate used of
0.00 gpd 0
Summary of Emissions are below:
Emission assumptions
Estimated total tank throughput gal/min 0.00 l!nits µ�
Estimated total tank throughput gal/day 0.00
ank Operation ays year 365
Annual Annual
Emissions Emissions Annual Emissions
Compound Sample Concentrations Units (lbs/hr) (lbs/year) (tons/yr)
Styrene''6 0.100 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
t-1,2-dichloroethene5 10.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
Fluorotrichloromethane5 10.000 µ 0.0000E+00 0.0000E+00 0.0000E+00
Trichloroethylene(trichloroethene)''6 0.005 µ 0.0000E+00 0.0000E+00 0.0000E+00
Vinyl acetateb 0.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
Vinyl chloride''6 0.002 µ 0.0000E+00 0.0000E+00 0.0000E+00
Xylenes''6 10.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
Benzene1'6 0.001 µ 0.0000E+00 0.0000E+00 0.0000E+00
Toluene"Toluene"6 1.000 µg/L 0.0000E+00 0.0000E+00 0.0000E+00
'Hazardous Air Pollutants listed in Title III of the 1990 Clean Air Act Amendments
'`Source tests did not indicate whether this compound was the para-or ortho-isomer.
The para isomer is a Title III-listed HAP.
3No data were available to speciate total Hg into the elemental and organic forms.
°Non-Volatile Organic Compounds(Non-VOCs)as indicated in 40 CFR 5 1.100
Compounds that are not in the National Priority Drinking Water Regulations MCL list. Because leachate is a
liquid,conservative assumption concentrations of 10 µg/L have been utilized.
6 Compounds are listed as both a HAP and are on the National Priority Drinking Water Regulations MCL list.
A conservative leachate sample concentration estimate of 1000 times the MCL(µg/L)has been used to estimate
emissions through volitization and evaporation.
Total VOCs
HAPs 0.000 tons/yr
Total VOCs
Non-Haps 0.000 tons/yr
Total Non-VOCs
HAPs 0.000 tons/yr
Total Non-VOCs
Non-Haps 0.000 tons/yr
Page 2

LEACHATE BASIN EMISSION SUMMARY
380,000 Gallon
Emissions from the leachate tanks were estimated based on comparison of National Priority Drinking Water
(MCL)concentrations of each pollutant. It has been assumed that all VOCs and TAPS in the leachate tank
influent evaporate.The average emissions(lbs/hr)were calculated by multiplying the concentration of each
pollutant by the estimated influent rate of leachate.
The estimated influent rate used of
14,577.35 gpd 5,320,734 gpy
Summary of Emissions are below:
Emission assumptions
Estimated total tank throughput gal/min 10.12 Units µag
Estimated total tank throughput gal/day 14,577.35
ank Operation ays year 365
INEENEEN
Annual nnua
or
Emissions Emissions Annual Emissions
Compound Sample Concentrations Units (lbs/hr) (lbs/year) (tons/yr)
1,1,1-Trichloroethane
(methyl chloroform)''4,6 0.200 µg/L 1.0137E-06 8.8803E-03 4.4402E-06
1,1,1,2-Tetrachloroethane''' 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
1,1,2,2-Tetrachloroethane''5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
1,1-Dichloroethane
(ethylidene dichloride)''5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
1,1,2 Trichloroethane''6 0.005 µg/L 2.5343E-08 2.2201E-04 1.1100E-07
1,2 Dichlorobenzene5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
1,1-Dichloroethene
(vinylidene chloride)''5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
1,2-Dichloroethane
(ethylene dichloride)''6 0.005 µg/L 2.5343E-08 2.2201E-04 1.1100E-07
1.2-Dichloropropane(propylene
dichloride)''6 0.005 µg/L 2.5343E-08 2.2201E-04 1.1100E-07
1.2-Dibromo-3-chloropropane6 0.000 µg/L 1.0137E-09 8.8803E-06 4.4402E-09
1,2 Dibromoethane''6 0.005 µg/L 2.5343E-08 2.2201E-04 1.1100E-07
1,4 Dichlorobenzene''6 0.600 µg/L 3.0412E-06 2.6641E-02 1.3320E-05
Acetones 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Acrylonitrile''' 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Bromocbloromethane5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Bromodichloromethane' 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Bromoform''5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Bromomethane''' 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Carbon disulfide''5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Carbon tetrachloride''6 0.005 µg/L 2.5343E-08 2.2201E-04 1.1100E-07
Chlorobenzene''6 0.100 µg/L 5.0687E-07 4.4402E-03 2.2201E-06
Chloroethane
(ethyl chloride)''' 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Chloroform''' 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Chloromethane5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Dibromochloromethane5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Dibromomethane5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
cis-1,2-Dichloroethene5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
cis-1,3 Dichloropropene5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
trans-1,3 Dichloropropene5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
trans-l,4-Dichloro-2-butene5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Dichloromethane
(methylene chloride)''4,6 0.005 µ 2.5343E-08 2.2201E-04 1.1100E-07
Ethylbenzene''6 0.700 µg/L 3.5481E-06 3.1081E-02 1.5541E-05
Iodomethane5 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
MEK' 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
MBK5 10.000 µg/L I 5.0687E-05 4.4402E-01 2.2201E-04
MIK5 10.000 99/1- 5.0687E-05 4.4402E-01 2.2201E-04
Perchloroethylene
(tetrachloroethylene)''4'6 0.005 µg/l- 2.5343E-03 2.2201E-04 1.1100E-07
Page 1

LEACHATE BASIN EMISSION SUMMARY
380,000 Gallon
Emissions from the leachate tanks were estimated based on comparison of National Priority Drinking Water
(MCL)concentrations of each pollutant. It has been assumed that all VOCs and TAPS in the leachate tank
influent evaporate.The average emissions(lbs/hr)were calculated by multiplying the concentration of each
pollutant by the estimated influent rate of leachate.
The estimated influent rate used of
14,577.35 gpd 5,320,734 gp�
Summary of Emissions are below:
Emission assumptions
Estimated total tank throughput gal/min 10.12 Units
Estimated total tank throughput gal/day 14,577.35
ank Operation ays year 365
Annual nua
Emissions Emissions Annual Emissions
Compound Sample Concentrations Units (lbs/hr) (lbs/year) (tons/yr)
Styrene''6 0.100 µg/L 5.0687E-07 4.4402E-03 2.2201E-06
t-1,2-dichloroethene- 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Fluorotrichloromethane' 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Trichloroethylene
(trichloroethene)''6 0.005 µg/L 2.5343E-08 2.2201E-04 1.1100E-07
Vinyl acetate6 0.000 µ 0.0000E+00 0.0000E+00 0.0000E+00
Vinyl chloride''6 0.002 µg/L 1.0137E-08 8.8803E-05 4.4402E-08
Xylenes'16 10.000 µg/L 5.0687E-05 4.4402E-01 2.2201E-04
Benzene''6 0.001 1 µg/L I 2.5343E-09 I 2.2201E-05 1 1.1100E-08
Toluene' 1.000 1 µg/L I 5.0687E-06 I 4.4402E-02 2.2201E-05
'Hazardous Air Pollutants listed in Title III of the 1990 Clean Air Act Amendments
2Source tests did not indicate whether this compound was the para-or ortho-isomer.
The para isomer is a Title III-listed HAP.
3No data were available to speciate total Hg into the elemental and organic forms.
°Non-Volatile Organic Compounds(Non-VOCs)as indicated in 40 CFR 5 1.100
5 Compounds that are not in the National Priority Drinking Water Regulations MCL list. Because leachate is a
liquid,conservative assumption concentrations of 10 µg/L have been utilized.
6 Compounds are fisted as both a HAP and are on the National Priority Drinking Water Regulations MCL list.
A conservative leachate sample concentration estimate of 1000 times the MCL(µg/L)has been used to estimate
emissions through volitization and evaporation.
Total VOCs
HAPs 0.003 tons/yr
Total VOCs
Non-Haps 0.003 tons/yr
Total Non-VOCs
HAPs 0.000 tons/yr
Total Non-VOCs
Non-Haps 0.000 tons/yr
Page 2

ACSWMF ABOVEGROUND STORAGE TANK EMISSIONS
Description of Tank Emission Point as VOC/HAP Emissions VOC/HAP Emissions
Referenced in Title V Application Tank Product (lbs/hr) (tons/year)
12,000 Gallon AST' Diesel(Off-Road) 0.0000E+00 0.0000E+00
12,000 Gallon AST' Diesel(On-Road) 6.8607E-04 3.0050E-03
250,000 Gallon AST Leachate 0.0000E+00 0.0000E+00
380,000 Gallon AST Leachate 7.7263E-04 3.3841E-03
500 Gallon AST' Gasoline 3.8531E-02 1.6877E-01
Total VOC/HAPs 3.9990E-02 0.1752
Note: 1. VOC/HAP emissions calculated using EPAs Tank 4.01d Program
2. Leachate tank emissions were calculated with the assumption of 100%volatility.Therefore,the emissions
associated with these tanks are more conservative than the output that would be produced by Tanks 4.01 d
Page 1

ATTACHMENT C
RESPONSIBLE OFFICIAL CHANGE LETTER

I
WASTE CONNECTIONS INC.
Connect with the Future°'
Anson Landfill
March 4,2016
Booker T.Pullen,Permit Engineer
North Carolina Department of Environmental Quality—Division of Air Quality
1641 Mail Service Center
Raleigh,NC 27699-1641
RE: Anson County Waste Management Facility,Raleigh,NC 27699-1641
Change in Responsible Official Notification
Air Quality Permit No.9835T03 Facility ID:0400052
Dear:Mr.Pullen:
On behalf of Anson County Waste Management Facility(ACWM),Franklin Engineers&Consultants,LLC.
(FE&C)is pleased to submit this letter to inform the North Carolina Department of Environmental Quality
(NCDEQ)that David Jones is no longer the Responsible Official. The following information represents the contact
information for the New Responsible Official:
Name: Tyler Fitzgerald
Title: District Manager
Work Phone: [phone]
Fax: [phone]
Mobile Phone: [phone]
Address: 375 Dozer Drive
Polkton,NC 28135
Tyler Fitzgerald's responsibilities and position satisfy the criteria to be considered a Responsible Official for a
Corporation as outlined in the definition of Responsible Official included in Part 70.2 which is stated below:
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 corporation,or a duly authorized representative of such person if the representative is responsible
for the overall operation of one or more manufacturing,production,or operating facilities applying for 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;
375 Dozer Drive, Polktoti. NC. 28135— Tel[phone]—Fax [phone]

WASTE CONNECTIONS INC.
Coxrnrt with she Future"
Anson Landfill
Tyler Fitzgerald will sign all future air reports,applications,letters,etc.as Responsible Official,as required. If you
have any questions regarding this notification,please contact Lana Brown at(901)500-1812 or me at(281)205-
8415.
Sincerely,
Anson County Waste Management Facility
David Jones
District Manager
Division of Air Quality—North Carolina Department of Environmental Quality(Fayetteville Regional Office)
Lana Brown—Waste Connections Environmental Compliance Specialist
Tyler Fitzgerald—Waste Connections District Manager
Juene Franklin—Franklin Engineers&Consultants,LLC.President
375 Dozer Drive, Polkton, NC. 28135— Tel[phone]—Fax [phone]