AQ_F_0800081_20110729_EI_Cmb-EI-File

I� WaRO Copy � �
:S✓
2010 Emissions Inventory Review/Data Tracking Form
Facility Name: pe�rwIu-e--
County/Premise Number: pe(,vpg/ Assigned to: Confidential? A6
Initial Review/Data Ent
NfA If Confidential information received,it has been properly labeled and stored. Sanitized copies
have been received for public use.
If the inventory was AERO submitted,DAQ received at least one hard copy of signatory form and
calculations that weren't provided in AERO.
/\(/A If the inventory was not AERO submitted, DAQ received a complete hard copy with signatory
form.
Invento Review/Database Entry
X Data appears to be complete x Calculations and control efficiencies
supporting emissions appear correct
i/ Calculations appear to add up ok ✓ All permitted sources and required
significant activities are quantified
NIA All compliance issues resulting from review are being addressed.(i.e.toxics,emission limitations
exceeded,unpermitted sources)
All volatile HAPS/TAPS are included in the VOC total
All appropriate ID numbers are entered where they should be(Source,Stack)
Comments: —)Pe- /7oIES ,-Yn Tco /l '"41, �CY�n /r L // �. le�''QK�c�
Sow toq 140 k7)c j, 4 e,�c -gn1%y Basle ne4l 7 PGi✓ �[ ��/je��
{'drrr7�..,Q�y d.Q � J��o w�i 1 r � h/C:/co� Cvr� �lcu�n-P ��e err/ sSlor►S G1 i�
5 d. s" /h �-6f�-2 J� Y cry vY /�c uo�✓,,. �1 Crfls s�cn✓ cr�r�c��pGcck o�
Sentbhu V/,kck JAA, d wl f� yl►� m� c ,✓ 6vl�vc spa .
71/b �/ Jn C-b j,,r n7' �daiF ColYr ,�`� 4/s D C-�2
Signature: C/71�yol SyS`fPi»�S
Date Emissions Data Approved in AERO and Complete in FEES
Don't forget to handle confidential files and data properly!

Facility Total CY 2010 Emission Summary Recorded in ED Facility ID #: 0800081
Facility Name: Perdue Farms Inc-Lewiston Permit#(s): 03085T28
Green House Gases Pollutants (GHG)
Actual missions
Tons/Yr /0 Change
Pollutant CAS CY 2010 CY 2009
from ED from Fees
Nitrous Oxide (N20) 10024977 0.096300 0.136900 -29.7%
Methane (CH4) 74-87_8 381.86 382.02 0.0%
Carbon Dioxide (CO2) 124389 42,015.56 42,990.38 -2.3%
CO2 equivalent(sum of individual GHG pollutant emission times their 45,418.50 metric tons
1995 IPCC Global Warming Potential (GWP), converted to metric tons)
Criteria Pollutants Actual Emissions % Change
(Tons/Year)
Pollutant CAS CY 2010 CY 2009
from ED from Fees
CO CO 30.30 28.26 7.2%
NOx Nox 42.81 53.69 -20.3%
PM(TSl ) '1'51 16.08 21.67 -25.8 /o
PM10 1'M 10 8.92 12.61 -29.3%
PM2.5 PM2.5 0.980000 5.02 -80.5%
S02 S02 11.68 108.10 -89.2%
VOC V0C 12.12 12.13 -0.1%
Hazardous Air Pollutants HAPs Actual Emissions 0/0 Change
and/or Toxic Air Pollutants (TAPs) (Pounds/Year)
Pollutant CAS CY 2010 CY 2009
from ED from Fees
Polycyclic Organic Matter(Specific Compounds from OAQPS for 0.611210 1.45 -57.8;';,
T
Benzo(a)pyrene (Component of 833291POMTV& 50-32-8 0.001210 0.001390 N/A
5655317PAH)
Naphthalene (Component of 833291POMTV) 91-20-3 0.610000 1 .45 -57.9%
Polycyclic Organic Matter(7 PAH Compounds for NIF) 0.001210 0.001390 N/A
07/29/2011 Page 1 of 4

Facility Total CY 2010 Emission Summary Recorded in ED Facility ID #: 0800081
Facility Name: Perdue Farms Inc- Lewiston Permit#(s): 03085128
Hazardous Air Pollutants (HAPs) Actual Emissions % Change
and/or Toxic Air Pollutants (TAPs) (Pounds/Year)
Pollutant CAS CY 2010 2009
from EDTromCY
Fees
Polycyclic Organic Matter (7 PAH Compounds for NIF) 0.001210 0.001390 N/A
Benzo(a)pyrene (Component of 833291POMTV& 50-32-8 0.001210 0.001390 N/A
5655317PAH)
Nickel& Compounds, sum total mass includes elemental 6.80 55.25 -87.7%
Nickel metal (Component of NIC) 7440-02-0 6.80 Not N/A
Reported
Nickel Unlisted Compounds (Component of NIC- N1C-other Not 55.25 N/A
Specify) Reported
Mercury & Compounds -all total mass includes Hg Vapor Not 0.073880 N/A
Reported
Mercury Unlisted Compounds - Specify Compound HGC-Other Not 0.073880 N/A
(Component of HGC) Reported
Manganese & compounds Not 1.96 N/A
Reported
Manganese Unlisted Compounds -Specify MNC-Other Not 1.96 N/A
Compound(Component of MNC) Reported
Lead& compounds Not 0.987340 N/A
Reported
Lead Unlisted Compounds -Specify Compound PBC-Other Not 0.987340 N/A
(Component of PBC) Reported
Cobalt& compounds Not 3.94 N/A
Reported
Cobalt Unlisted Compounds -Specify Compound COC-Other Not 3.94 N/A
(Component of COC) Reported
Chromium (VI) Non-Specific Compounds, as Chrom(VI) Not 0.552520 N/A
(Component CRC Reported
Chromium (VI) Non-Specific Unlisted Compounds - NSCR6-Other Not 0.552520 N/A
Specify Compound(Component of NSCR6& CRC) Reported
Chromium -All/Total(includes Chromium (VI) categories, metal Not 0.552520 N/A
and others) Reported
Chromium (VI) Non-Specific Unlisted Compounds - NSCR6-Other Not 0.552520 NIA
Specify Compound(Component of NSCR6& CRC) Reported
07/29/201 1 Page 2 of 4

Facility Total CY 2010 Emission Summary Recorded in ED Facility ID #: 0800081
Facility Name: Perdue Farms Inc- Lewiston Permit#(s): 03085T28
Hazardous Air Pollutants (HAPs) Actual Emissions % Change
and/or Toxic Air Pollutants (TAPS) (Pounds/Year)
Pollutant CAS CY 2010 TCY 2009
from EDm Fees
Cadmium & compounds (total mass includes elemental metal) Not 0.260240 N/A
Re orted
Cadmium Unlisted Compounds -Specify Compound CDC-Other Not 0.260240 N/A
(Component of CDC) Reported
Beryllium & compounds (Total mass) Not 0.018180 N/A
Reported
Beryllium Unlisted Compounds -Specify Compound BEC-Other Not 0.018180 N/A
(Component of BEC) Reported
Arsenic & Compounds (total mass of elemental AS, arsine and all Not 0.863100 N/A
inorganic compounds) Reported
Arsenic Unlisted Compounds - Specify Compound ASC-Other Not 0.863100 N/A
(Component of ASQ Reported
Antimony & Compounds (total mass, inc elemental SB) Not 3.43 N/A
Reported
Antimony Unlisted Compounds - Specify Compound SBC-other Not 3.43 N/A
(Component of SBC) Reported
Acetaldehyde 75-07-0 0.118000 0.136000 -13.2%
Acrolein 107-02-8 0.037000 0.043000 -14.0%
Ammonia(as NH3) 7664-41-7 13,758.00 22,169.00 -37.90/0
Benzene 71-43-2 5.00 5.53 -9.7%
Ethyl benzene 100-41-4 Not 0.041580 N/A
Reported
Fluorides (sum of all fluoride compounds as mass of 16984-48-8 3.00 24.39 -87.7%
F ion)
Formaldehyde 50-00-0 52.98 71.09 -25.5`0
Hexane, n- 110-54-3 1,183.00 1,027.30 15.20/0
Methyl chloroform 71-55-6 Not 0.154320 N/A
Reported
Phosphorus Metal, Yellow or White 7723-14-0 Not 6.19 N/A
Reported
07/29/201 1 Page 3 of 4

Facility Total CY 2010 Emission Summary Recorded in ED Facility ID #: 0800081
Facility Name: Perdue Farms Inc- Lewiston Permit#(s): 03085T28
Hazardous Air Pollutants(HAPs) Actual Emissions '% Change
and/or Toxic Air Pollutants (TAPs) (Pounds/Year)
Pollutant CAS CY 2010 CY 2009
from ED from Fees
Polycyclic Organic Matter(Inc PAH, dioxins, etc. POM 1.00 1.92 -48.0'%,
NC & AP 42 historic)
Selenium Compounds SEC Not 0.446600 N/:1
Reported
Toluene 108-88-3 3.56 5.57 -36.1'io
Trichloroethane, 1,1,2- 79-00-5 Not Not N/A
Reported Reported
Xylene, o- 9>47-6 0.900000 1.11 -19.0%
Largest Individual HAP Hexane, n- 1,183.00 lbs
Total HAP Emissions 1,254.00 lbs
('ri fits c,
DA_4's Comments Regarding Inventory Z�9 `>°�/wco� o��
Cer�ay-1
I added formaldehyde,flourides,toluene and nickel to the HAP list and CC2 GHG from boilers'fuel oil combustion The
rest of the boiler HAPs that are not reported in ED are less than 0.5 lb. The emission factor that Perdue uses for poultry
conveyance and loadout is high(AP-42 grain),but there are no other factors I know of to apply. The meal is moist,so
there should be very low to negligible emissions I made significant changes to the structure of the data All of the meal
silo bagfilters were grouped together. The cookers,evaporators and press were grouped together. The receiving and
handling bagfilters were grouped I had to clean up the stack data and control device systems Links in the OS to control
systems and stacks were also corrected I had Perdue go back and look at stack parameters to make sure all was correct(it
appeared that they might not have updated data when new venturi and packed scrubbers were installed.
07/29/2011 Page 4 of 4

Huddleston, Betsy
From: Baggett, Joey [[e-mail]
Sent: Thursday, September 22, 2011 3:18 PM
To: Huddleston, Betsy
Subject: Annual Emissons Inventory
Question„ I have entered AERO and made the changes to the Anaerobic pond methane calculations. Do I need to mail
you a new hard copy of the whole thing, do I need to send another Certification statement.
What do I need to do besides submit it on AERO which I have done.
Thanks,
Joey Baggeu
Perdue Agribusiness
Environmental
252-287-5196
This communication,including attachments,may contain confidential,privileged,copyrighted or other legally protected information.If you are not the intended
recipient,you are hereby notified that any use.disclosure,dissemination,distribution,or copying of this communication,or any of its contents,is strictly prohibited.
If you have received this communication in error,please immediately re-send this communication to the sender and delete the original message and any copy of it.
including all attachments,from your computer system.
1

Huddleston, Betsy
From: Baggett, Joey [[e-mail]]
Sent: Tuesday, July 19, 2011 5:13 PM
To: Huddleston, Betsy
Subject: RE: Poultry meal loadout
The loaduot is only ten percent controlled, ninety percent uncontrolled. If you use ten percent efficiency the TSP would
go from 11567.04 lbs. to 1,285.23 lbs.
The .27 is a soybean meal factor, this is the one that maybe should be less .
The WW methane comes from a earl gallons effluent number and the amount of COD per pound. This was done in
yearly p
2009.The AERO format would not let me change it at all.
From: Huddleston, Betsy [mailto:[e-mail]
Sent: Tuesday, July 19, 2011 3:58 PM
To: Baggett, Joey
Subject: Poultry meal loadout
The poultry meal loadout uses an emission factor of 0.27 lb/ton. The control efficiency is listed a 0.9. 1 assume you mean
90%control due to the meal being moist and little loss? If so,the control efficiency should be 0.1 in the column. Please
let me know what to do here.
Betsy Huddleston, Environmental Engineer II
NCDENR, Division of Air Quality
Washington Regional Office
943 Washington Sq. Mall, Washington,NC 27889
Phone: [phone]
Fax: [phone]
http://www.ncair.org
************************************************************************
Email correspondence to and from this address is subject to the North Carolina
Public Records Law and may be disclosed to third parties unless the content is exempt by
statute or other regulation.
************************************************************************
'This communication,including attachments,may contain confidential,privileged,copyrighted or other legally protected information.if you are not the intended
recipient,you are hereby notified that any use,disclosure,dissemination,distribution,or copying of this communication,or any of its contents.is strictly prohibited.
If you have received this communication in error,please immediately re-send this communication to the sender and delete the original message and any copy of it,
including all attachments,from your computer system.
1

Huddleston, Betsy
From: Baggett, Joey [[e-mail]]
Sent: Friday, July 22, 2011 11:56 AM
To: Huddleston, Betsy
Subject: RE: Lewiston Inventory Questions
I hope I've helped some. I guess Wayne set these up originaly.
The fire pump in Cofield is supposed to be used only for emergency.
From: Huddleston, Betsy Imailto:[e-mail]
Sent: Thursday, July 21, 2011 12:04 PM
To: Baggett, Joey
Subject: Lewiston Inventory Questions
Hi Joey,
I need another favor from you. There are several data items that I need you to look at and confirm or correct:
1. What is the estimated control efficiency of the venturi, crossflow scrubber and packed tower scrubber
combination for VOC from the process being collected? My estimate is 80%?
2. Please check the following stack parameters(flows seem low or don't jive when you try to calculate-want to re-
verify): 80 percent for the packed tower S02 , 94 percent for PM,46 percent for PM in the crossflow& 80
percent Pm for the venturi
a. Crossflow scrubber-62.5 ft high, (5 ft. diameter) 1.18 ft diameter, 93 degrees,velocity 43.3, ( 118,200
acfm ) 2841.14 acfm
b. Backup boiler-1764 acfm, 6.5 ft/s ?
c. ES-4 and 5, 19.1 ft/s, 3600 acfm ?
d. Packed scrubber-50 ft high, (2.167 ft diameter) 3.9 ft diameter,490 temp, 6.48 ft/s, (48,000 acfm ) 4658
acfm , 37.2 ft/sec velocity
e. Poultry meal conveyance 0.42 diameter, 59.5 ft/s,494.6 acfm , I could not find any numbers for these, but
they are enclosed pneumatic lines
I've made the following changes to the database that should help you when completing inventory next year:
1. The meal silos are all in one group.You can report their combined emission.
2. 1 grouped the meat and feather cookers,evaporators and presses in one group.
3. 1 reviewed the existing control device systems. I cleaned up the ones for the cookers/evap/presses, silos,
rendering room air and rendering boilers.
Betsy Huddleston, Environmental Engineer II
NCDENR, Division of Air Quality
Washington Regional Office
943 Washington Sq. Mall, Washington, NC 27889
Phone: [phone]
Fax: [phone]
http://www.ncair.org
************************************************************************
Email correspondence to and from this address is subject to the North Carolina
I

Huddleston, Betsy
From: Huddleston, Betsy
Sent: Thursday, July 21, 2011 12:51 PM
To: 'Baggett, Joey'
Subject: One more grouping
I also grouped all the live receiving and handling baghouses together.
Betsy Huddleston, Environmental Engineer II
NCDENR, Division of Air Quality
Washington Regional Office
943 Washington Sq. Mall, Washington,NC 27889
Phone: [phone]
Fax: [phone]
http://www.ncair.org
************************************************************************
Email correspondence to and from this address is subject to the North Carolina
Public Records Law and may be disclosed to third parties unless the content is exempt by
statute or other regulation.
************************************************************************
1

NATURAL GAS COMBUSTION EMISSIONS CALCULATOR REVISION H 5/24/2010-OUTPUT SCREEN
Instructions: Enter emission source I facility data on the"INPUT'tab/screen. The air emission results and summary of Input data are viewed/
PWA printed on the"OUTPUT"tablscreen. The different tabs are on the bottom of this screen.
ACI
This spreadsheet is for your use only and should be used with caution.DENR does not guarantee the accuracy of the Information contained. This
NCDENR spreadsheet is subject to continual revision and updating. It is your responsibility to be aware of the most current information available. DENR Is
not responsible for errors or omissions that may be contained herein.
SOUR E/FACILITY/USER INPUT SUMMARY FROM INPUT SCREEN
COMPANY. Perdue Farms Inc. FACILITY ID NO.. 800081
PERMIT NUMBER: 03085T28
EMISSION SOURCE DESCRIPTION: 20.3 MMBTU/HR NATURAL GAS-FIRED BOILER FACILITY CITY: Lewiston
EMISSION SOURCE ID NO.: ES4 FACILITY COUNTY: Bartle
CONTROL DEVICE: I NO CONTROL POLLUTANT I CONTROLEFF.
SPREADSHEET PREPARED BY: Joey Baggett NOX CALC'D AS 0
ACTUAL FUEL THROUGHPUT: 65.59 10 SCF/YR FUEL HEAT VALUE: 1,020 BTU/SCF
POTENTIAL FUEL THROUGHPUT: 174.34 10 SCF/YR BOILER TYPE: SMALL BOILER <100 mmBTUMR
REOUESTED MAX.FUEL THRPT: 0.00 10 SCF/YR NO SNCR APPLIED
CRITERIA AIR POLLUTANT EMISSIONS INFORMATION
ACTUAL EMISSIONS POTENTIAL EMISSIONS EMISSION FACTOR
yFTER CONTROLS I UNITS) (BEFORE CONTROLS I LMiS) tI, .CONTams,LIMITS) Ib✓mmBtu
AIR POLLUTANT EMITTED Whir tonstyr Ib/hr tonstyr Whir tan uncontrolled controlled
PARTICULATE MATTER Total 0.15 0.25 0.15 0.66 0.15 0.00 0.007 0.007
PARTICULATE MATTER Condensable 0.11 0.19 0.11 0.50 0.11 0.00 0.006 0.006
PARTICULATE MATTER Filterable 0.04 0.06 0.04 0.17 0.04 0.00 0,002 0.002
SULFUR DIOXIDE S02 0.01 0.02 0.01 0.05 0.01 0.00 0.001 0.001
NITROGEN OXIDES NOx 1.99 3.28 1.99 8.72 1.99 0.00 0.098 0.098
CARBON MONOXIDE CO 1.67 2.75 1.67 7.32 1.67 0.00 0.082 0.082
VOLATILE ORGANIC COMPOUNDS VOC 0.11 0.18 0.11 0.48 0.11 0.00 0.005 6.005
LEAD 9.95E-06 1.6E-OS 1.0E-05 4.4E-05 1.0E-05 0.0E+00 4.9E-07 4.9E-07
TOXIC/HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION
ACTUAL EMISSIONS POTENTIAL EMISSIONS EMISSION FACTOR
CAS (AFTER CONTROLS I LIMITS) (BEFORECONTROLSIUMITS) (AFTER CONTROLS I LIMBS) Ib/mmBtu
TOXIC I HAZARDOUS AIR POLLUTANT NUMBER Ib/hr I r Ib/hr INhr bey uncontrolled controlled
Arsenic&Compounds TH ASC 0.00ETOO- O.00E+00 0.00E+00 O.00E+00 0.00E+00 0.00E+00 0.00E+00 D o0E+00
Benzene H 71432 4.18E-05 1.38E-01 4.18E-05 3.66E-01 4.18E-05 0.00E+00 2.06E-0s 2.06E-06
Benzo a rene H 50328 2.39E-08 7.87E-05 2.39E-08 2.09E-04 2.39E-08 O.00E+00 1.18E-09 1.18E-09
Beryllium metal H 7440417 0.00E+00 O.00E+00 O.00E+00 O.00E+00 O.00E+00 O.00E+00 0.o0E+00 0.00E+00
Cadmium&compounds TH CDC 0.00E+00 0.00E+00 0.00E+00 0.00E+00 O.00E+00 0.00E+00 O.DDE+00 o.DOE+00
Chromium-All/Total H CRC O.00E+00 O.00E+00 0.00E+00 O.00E+00 O.00E+00 O.00E+00 0.o0E+00 0.00E+00
Soluble Chromate Compounds,as Chromium I H SOICR6 0.00E+00 0.00E+00 O.00E+00 0.00E+00 O.00E+00 0.00E+00 0.00E+00 o.DOE+00
Cobalt compounds H COC 1.67E-06 5.51E-03 1.67E-06 1.46E-02 1.67E-06 O.00E+00 8.24E-0e 8.24E-De
Formaldehyde H 50000 1.49E-03 4.92E+00 1.49E-03 1.31E+01 1.49E-03 0.00E+00 7.35E-05 7.35E-05
Hexane,n- TH 110543 3.58E-02 1.18E+02 3.58E-02 3.14E+02 3.58E-02 0.00E+00 1.76E-03 1.76E-03
Man anese&Com ounds H MNC O.00E+00 O.00E+00 O.00E+00 0.00E+00 O.00E+00 0.00E+00 000E+00 o.DOE+00
Mercury &Compounds TH HGC O.00E+00 O.00E+00 0.00E+00 O.00E+00 O.00E+00 O.00E+00 0 OOE+00 0.00E+0D
Na thalene H 91203 1.21E-05 4.00E-02 1.21E-05 1.06E-01 1.21E-05 0.00E+00 5.98E-07 5.98E-07
Nickel metal H 7440020 0.00E+00 0.00E+00 0.00E+00 O.00E+00 O.00E+00 O.00E+00 0 00E+00 o.00E+oo
Selenium compounds H SEC 4.78E-07 1.57E-03 4.78E-07 4.18E-03 4.78E-07 O.00E+00 2.35E-08 2.35E-0e
Toluene TH 108883 1 6.77E-05 I 2.23E-01 I 6.77E-05 5.93E-01 6.77E-05 I 0.00E+00 I 3.33E-06 3.33E 06
Total HAPs 3.74E-02 1.23E+02 3 74E-02 I 3.28E+02 I 3.74E-02 I 0.00E+00 1 1.s4E-03 184E-03
Highest HAP Hexane I 3.58E-02 1.18E+02 3 58E-02 I 3.14E+02 I 3.58E-02 I O.00E+00 1 1 76E-031 1 76E-03
TOXIC AIR POLLUTANT EMISSIONS INFORMATION OR PERMITTING PURPOSES
EXPECTED ACTUAL EMISSIONS AFTER CONTROLS/LIMITATIONS EMISSION FACTOR
Ib/mmBtu
TOXIC AIR POLLUTANT CAS Num. ib/hr lb/day Ib/r uncontrolled controlled
Arsenic&Compounds TH ASC O.00E+00 O.00E+00 0.00E+00 0.00E+00 0.00E+00
Benzene TH 71432 4.18E-05 1.00E-03 0.00E+00 2.D6E-06 2.06E-06
Benzo a rene TH 50328 2.39E-08 5 73E-07 0.00E+00 1.18E-09 1.1eE-o9
Beryllium metal H 7440417 O.00E+00 0 00E+00 0.00E+00 0.00E+00 0.00E+00
Cadmium&compounds TH CDC 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00
Soluble Chromate Compounds,as Chromium I So1CR6 O.00E+00 O.00E+00 O.00E+00 0.00E+0o 0.00E+00
Formaldehyde TH 50000 1.49E-03 3.58E-02 O.00E+00 7.35E-05 7.35E-05
Hexane n- H _ 110543 3.58E-02 8.60E-01 O.00E+00 1.76E-03 1.76E-03
Manganese&Compounds TH MNC O.00E+00 0.00E+00 O.00E+00 0.00E+00 0.00E+oo
Mercury &Compounds H HGC 0.00E+00 0.00E+00 0.00E+00 000E+00 0.00E+00
Nickel metal TH 7440020 0.00E+00 0.00E+00 0.00E+00 0 00E+00 0.00E+001
Toluene(TH) 108883 6.77E-05 1 82E-03 0.00E+00 3 33E-06 3 33E-06
GREENHOUSE GAS EMISSIONS INFORMATION(FOR EMISSIONS INVENTORY PURPOSES) -CONSISTENT WITH EPA MANDATORY REPORTING GHG-POTENTIAL TO EMIT
RULE(MRR)METHOD NOT BASED ON EPA MRR METHOD
GREENHOUSE GAS POLLUTANT ACTUAL EMISSIONS POTENTIAL EMISSIONS
EPA MRR CALCULATION METHOD:TIER 1
metric tons/yr metric tons/yr,CO2e short tonstyr short tons/yr short tons/yr,CO29
CARBON DIOXIDE(CO2) 3574.95 3,574.95 3,940.71 10.393.06 10393.06
METHANE(CH4) 6.74E-02 1.42E+00 7.43E-02 1.96E-01 4.12E+00
NITROUS OXIDE(N20) 6.74E-03 2.09E+00 7 43E-03 1.96E-02 6.08E+00
TOTAL CO2e 3,578.48 TOTAL CO2e 10,403.26
NOTE: CO2e means CO2 equivalent metric tons) short tons

NATURAL GAS COMBUSTION EMISSIONS CALCULATOR REVISION H 5/24/2010-OUTPUT SCREEN
Instructions: Enter emission source/facility data on the"INPUT'tablscreen. The air emission results and summary of Input data are viewed/
printed on the"OUTPUT"tab/screen. The different tabs are on the bottom of this screen.
This spreadsheet is for your use only and should be used with caution.DENR does not guarantee the accuracy of the information contained. This
NCDENR spreadsheet is subject to continual revision and updating. It is your responsibility to be aware of the most current Information available. DENR Is
not responsible for errors or omissions that may be contained herein.
SOURCE/FACILITY/USER INPUT SUMMARY FROM INPUT SCREEN
COMPANY. Perdue Farms Inc. FACILITY ID NO.. 800081
PERMIT NUMBER: 03085T28
EMISSION SOURCE DESCRIPTION: 20.3 MMBTU/HR NATURAL GAS-FIRED BOILER FACILITY CITY: Lewiston
EMISSION SOURCE ID NO.: ES-5 FACILITY COUNTY: Bertie
CONTROL DEVICE: I NO CONTROL POLLUTANT I CONTROL EFF.
SPREADSHEET PREPARED BY: Joey Baggett NOX CALC'D AS 0%
ACTUAL FUEL THROUGHPUT: 65.59 10 SCF/YR FUEL HEAT VALUE: 1,020 BTU/SCF
POTENTIAL FUEL THROUGHPUT: 174.34 10 SCF/YR BOILER TYPE: SMALL BOILER <100 mmBTU/HR
REQUESTED MAX.FUEL THRPT: 0.00 10 SCF/YR NO SNCR APPLIED
CRITERIA AIR POLLUTANT EMISSIONS INFORMATION
ACTUAL EMISSIONS POTENTIAL EMSSIONS EMISSION FACTOR
(AFTER CONTROLS I La8T8) MEFd CONTROLS I LIMITS) (IFIER CCNTRCLS I OMITS) IbtmmBtu
AIR POLLUTANT EMITTED Whir tonstyr Ib/hr tons/yr Ib/hr tons/yr uncontrolled controlled
PARTICULATE MATTER Total 0.15 0.25 0.15 0.66 0.15 0.00 0.007 0.007
PARTICULATE MATTER Condensable 0.11 0.19 0.11 0.50 0.11 0.00 0.006 0.006
PARTICULATE MATTER Filterable 0.04 0.06 0.04 0.17 0.04 0.00 0.DO2 0.002
SULFUR DIOXIDE S02 0.01 0.02 0.01 0.05 0.01 0.00 0.001 0.001
NITROGEN OXIDES NOx 1.99 3.28 1.99 8.72 1.99 0.00 0.D98 0.098
CARBON MONOXIDE CO 1.67 2.75 1.67 7.32 1.67 0.00 0.082 0.082
VOLATILE ORGANIC COMPOUNDS VOC 0.11 0.18 J. 0.48 0.11 0.00 0.005 0.005
LEAD 9 95E-06 1.6E-05 1.0E-05 4 4E-05 1.DE-051 0.0E+00 4.9E-07 4.9E-07
TOXIC/HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION
ACTUAL EMISSIONS POTENTIAL EMSSIONS EMISSION FACTOR
CAS (AFTERCONTROLSIIIMITS) (9EFOREC0NTROLSIUMITS) (A+TERCONTROLSIIJWTS) Ibi-Eltu
TOXIC I HAZARDOUS AIR POLLUTANT NUMBER Ib/hr lbelyr Ihlhr lbstyr Ibfhr lbetyr uncontrolled controlled
Arsenic&Compounds TH ASC 0.00E+00 O.00E+00 O.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.20E+00
Benzene H 71432 4.18E-05 1.38E-01 4.18E-05 3.66E-01 4.18E-05 O.00E+00 2.06E-06 2.06E-06
Benzo a rene TH 50328 2.39E-08 7.87E-05 2.39E-08 2.09E-04 2.39E-08 0.00E+00 1.18E-09 1.18E-09
Beryllium metal TH 7440417 O.00E+00 0.00E+00 O.00E+00 O.00E+00 0.00E+00 O.00E+00 0.00E+00 o.00E+00
Cadmium&compounds H CDC O.00E+00 O.00E+00 O.00E+00 O.00E+OO 0.00E+00 O.00E+00 0.o0E+00 O.00E+00
Chromium-AII/Total H CRC O.00E+00 0.00E+00 O.00E+00 O.00E+00 O.00E+00 0.00E+00 0.00E+00 2.O2E+oo
Soluble Chromate Compounds,as Chromium I H SoICR6 0.00E+00 0.00E+00 O.ODE+00 0.00E+00 O.00E+00 0.00E+00 O.o2E+00 0.00E+00
Cobalt compounds H COC 1.67E-06 5.51E-03 167E-06 1.46E-02 1.67E-06 0.00E+00 8.24E-08 8.24E-08
Formaldehyde H 50000 1.49E-03 4.92E+00 1.49E-03 1.31E+01 1.49E-03 0.00E+00 7.35E-05 7.35E-05
Hexane n- TH 110543 3.58E-02 1.18E+02 3.58E-02 3.14E+02 3.58E-02 O.00E+00 1.76E-03 1.76E-03
Manganese&compounds H MNC O.00E+00 0.00E+00 0.00E+00 O.00E+00 O.00E+00 O.00E+00 O.o2E+00 O.00E+00
Mercury &Compounds H HGC O.00E+00 O.o0E+00 O.DOE+00 0.00E+00 O.00E+00 O.00E+00 0.00E+0o 000E+00
Na thalene H 91203 1.21E-05 4.00E-02 1.21E-05 1.06E-01 1.21E-05 O.00E+00 5.98E-07 5.98E-07
Nickel metal H 7440020 0.00E+00 O.00E+00 O.00E+00 O.00E+00 0.00E+00 O.00E+00 0.00E+00 0.00E+00
Selenium compounds H SEC I 4.78E-07 I1.57E-03 4.78E-07 4.18E-03 4.78E-07 O.00E+00 2.35E-OB 2.35E-08
Toluene H 108883 6.77E-05 2.23E-01 6.77E-05 5.93E-01 6.77E-05 I 0.00E+00 3 33E-06 3.33E-26
Total HAPs 3.74E-02 1.23E+02 I 3.74E-02 3.28E+02 3.74E-02 I 0.00E+00 1.84E 03 1.84E-03
Highest HAP JHexane 1 3.58E-02 1.18E+02 I 3.58E-02 3.14E+02 3.58E-02 I 0.00E+00 1 76E-03 1 76E-03
TOXIC AIR POLLUTANT EMISSIONS INFORMATION OR PERMITTING PURPOSES
EXPECTED ACTUAL EMISSIONS AFTER CONTROLS/LIMITATIONS EMISSION FACTOR
Ib/mmBtu
TOXIC AIR POLLUTANT CAS Num. Ib/hr lb/day Iblyr uncontrolled controlled
Arsenic&Compounds H ASC O.00E+00 O.DOE+00 0.00E+00 O.00E+00 0.00E+02
Benzene H 71432 4.18E-05 1.00E-03 O.00E+00 2.06E-06 2.06E-06
Benzo a rene TH 50328 2.39E-08 5.73E-07 0.00E+00 1.18E-09 1 18E-09
Beryllium metal TH 7440417 0.00E+00 0.00E+00 O.00E+00 0.o0E+00 2.00E+00
Cadmium&compounds TH CDC 0.00E+00 0.00E+00 O.00E+00 0.a0E+o0 OoGE+00
Soluble Chromate Compounds,as Chromium VI TH SoICR6 O.OQE+00 O.00E+00 O.00E+00 0.00E+22 2.02E+00
Formaldehyde H 50000 1.49E-03 3.58E-02 0.00E+00 7.35E-05 7.35E-05
Hexane n- TH 110543 1 3.58E-02 8.60E-01 O.00E+00 1.76E-03 1.76E-03
Man anese&com unds H MNC 0.00E+00 0.00E+0p O.00E+00 0.00E+00 o.00E+00
Mercury &Compounds H HGC 0.00E+00 0.00E+00 0.00E+00 0.00E+0a ffl
Nickel metal TH 7440020 0.00E+00 0.00E+00 0.00E+00 0.00E+00
Toluene(TH 108883 6.77E-05 1.62E-03 0.OQE+00 3.33E-06
GREENHOUSE GAS EMISSIONS INFORMATION(FOR EMISSIONS INVENTORY PURPOSES) -CONSISTENT N9TH EPA MANDATORY REPORTING GHG-POTENTIAL TO EMIT
RULE(MRR)METHOD NOT BASED ON EPA MRR METHOD
GREENHOUSE GAS POLLUTANT ACTUAL EMISSIONS
EPA MRR CALCULATION METHOD.TIER 1 POTENTIAL EMISSIONS
metric tons/yr metric tons/yr,CO2a short tons/yr short tons/yr short tons/yr,CO2e
CARBON DIOXIDE(CO2) 3574.95 3,574.95 3,940.71 10,393.06 10393.06
METHANE(CH4) 6.74E-02 1.42E+00 7.43E-02 1.96E-01 4.12E+00
NITROUS OXIDE(N20) 6.74E-03 2.09E+00 7.43E-03 1.96E-02 6.08E+00
TOTAL CO2e 1 3,678.46 TOTAL CO2e 10,403.26
NOTE: CO2e means CO2 equivalent metric tonsshort tons

FUEL OIL COMBUSTION EMISSIONS CALCULATOR REVISION E 2/1/2010-OUTPUT SCREEN
Instructions: Enter emission source I facility data on the'9NPUT'tablscreen. The air emission results and summary of input data
are viewed I printed on the"OUTPUT'tab/screen. The different tabs are on the bottom of this screen.
A'F,5%
-_ This spreadsheet is for your use only and should be used with caution.DENR does not guarantee the accuracy of the Information contained.This spreadsheet
NCDENR Is subJect to continual revision and updating.It is your responsibility to be aware of the most current Information available.DENR Is not responsible for errors
or omissions that may be contained herein.
SOURCE/FA ILf Y/USER INPUT SUMMARY ROM INPUT SCREEN
COMPANY. Perdue Farms Inc. MAX HEAT INPUT. 84.00 MMBTU/HR
FACILITY ID NO.: 800081 FUEL HEAT VALUE: 150.000 BTU/GAL
PERMIT NUMBER: 03085T28 HHV for GHG CALCULATIONS: 0.150 mm BTU/GAL
FACILITY CITY: Lewiston ACTUAL ANNUAL FUEL USAGE: 41.077 GAL/YR
FACILITY COUNTY: Bertie MAXIMUM ANNUAL FUEL USAGE: 4.905,600 GAL/YR
USER NAME: Joey Baggett MAXIMUM SULFUR CONTENT- 1.8 %
EMISSION SOURCE DESCRIPTION: No 6 oil fired boiler REQUESTED PERMIT LIMITATIONS
EMISSION SOURCE ID NO.: ES8 MAX.FUEL USAGE: 0 GAL/YR
MAX.SULFUR CONTENT: 1.77 %
TYPE OF TROL DEVICES POLLUTANT CONTROL EFF.
SCRUBBER PM 0.94
NONE/OTHER S02 0.7
NONE/OTHER NOx 0
METHOD USED TO COMPUTE ACTUAL GHG EMISSIONS. TIER 1. DEFAULT HIGH HEAT VALUE AND DEFAULT EF
CARBON CONTENT USED FOR GHGS k C/al: CARBON CONTENT NOT USED FOR CALCULATION TIER CHOSEN
CIWIEW AIR POLLUTANT EMISSIONS INFORMATION
ACTUAL EMISSIONS POTENTIAL EM SSIONS EMISSION FACTOR
RA ER CONTROLS LIMITS, (BEFORE CONTROLS I LMTS) (AFTER CONTROLS lLMTS (III b/10' a
AIR POLLUTANT EMITTED Ib/hr tons/r Whir tonstyr Iblhr I tonstyr uncontrolled controlled
TOTAL PARTICULATE MATTER PM FPM+CPM 11.64 0.43 11.75 51.48 0.00 1 0.00 2.10E+01 2.08E+01
FILTERABLE PM(FPM) 10.81 0.40 10.91 47.80 0.00 1 0.00 1.95E+01 1.93E+01
CONDENSABLE PM CPM 0.83 0.03 0.84 3.68 0.00 0.00 1.50E+00 1.49E+00
FILTERABLE PM<10 MICRONS(PM1o) 9.36 0.34 9.45 41.37 0.00 0.00 1.69E+01 1.67E+01
FILTERABLE PM<2.5 MICRONS(PM2.5) 6.09 0.22 6.15 26.95 0.00 0.00 1.10E+01 1.09E+01
SULFUR DIOXIDE(S02) 154.53 5.67 155.62 881.61 0.00 0.00 2.78E+02 2.76E+02
NITROGEN OXIDES(NOJ 30.80 1.13 30.80 134.90 0.00 0.00 5.50E+01 5.50E+01
CARBON MONOXIDE(CO) 2.80 0.10 2.80 12.26 0.00 0.00 5.00E+00 5.00E+00
VOLATILE ORGANIC COMPOUNDS VOC 0.16 0.01 0.16 0.69 0.00 0.00 2.80E-01 2.80E-01
LEAD 0.00 0.00 0.00 0,00 0.00 0.00 1.51E-03 1.50E-03
ACTUAL EMISSIONS POTENTIAL EMSSIONS EMISSION FACTOR
CAB CONTROLS l-s) (9EFORE CONTROLS 1-5) (AFTER CONTROLe I U.eT Ib/10' al
TOXIC/HAZARDOUS AIR POLLUTANT NUMBER b 1hr r Ib/hr lbtvr IWhr I uncontrolled controlled
Antimony 8compounds H BBC 2.9E-03 2.1E-01 2.9E-03 2.6E+01 0.0E+00 O.0E+00 5.25E-03 5.20E-03
Arsenic 8 compounds ABC 7.3E-04 5.4E-02 7.4E-04 6.5E+00 0.0E+00 0.0E+00 1.32E-03 1.31E-03
Benzene TH 71432 1.2E-04 8.8E-03 1.2E-04 1.0E+00 0.0E+00 0.0E+00 2.14E-04 2.14E-04
Beryllium S compounds H BEC 1.5E-05 1.1E-03 1.6E-05 1.4E-01 0.0E+00 0.0E+00 2.78E-05 2.75E-05
Cadium 8 compounds TH CDC 2.2E-04 1.6E-02 2.2E-04 2.0E+00 0.0E+00 0.0E+00 3.98E-04 3.94E-04
Chromium-Allrrotal H CRC I 4.7E-04 3.4E-02 4.7E-04 4.1E+00 0.0E+00 0.0E+00 8.45E-04 8.37E-04
Cobalt compounds H CDC 3.3E-03 2.4E-01 I 3.4E-03 3.0E+01 0.0E+00 0.0E+00 6.02E-03 5.96E-03
Eth lbomene H 100414 3.6E-05 2.6E-03 I 3.6E-05 3.1E-01 1 O.0E+00 I O.0E+00 6.36E-05 6.36E-05
Fluorides sum fluoride compounds) T 16984488 2.1E-02 1.5E+00 1 2.1E-02 1.8E+02 0.0E+00 I 0.0E+00 3.73E-02 3.73E-02
Formaldehyde 50000 2.4E-02 1.7E+00 I 2.4E-02 2.1E+02 0.0E+00 0.0E+00 4.25E-02 4.25E-02
Lead and Lead compounds H PBC 8.4E-04 6.1 E-02 8.5E-04 7.4E+00 0.0E+00 0.0E+00 1.51E-03 1.50E-03
Manganese 8compounds TH MNC 1.7E-03 1.2E-01 1.7E-03 1.5E+01 0.0E+00 O.0E+00 3.00E-03 2.97E-03
Mercury8 compounds HGC 6.3E-05 4.6E-03 6.3E-05 5.5E-01 0.0E+00 0.0E+00 1.13E-04 1.13E-04
Methyl chloroform TH 71566 1.3E-04 9.7E-03 1.3E-04 1.2E+00 0.0E+00 0.0E+00 2.36E-04 2.36E-04
Na halene H 91203 8.3E-04 4.6E-02 6.3E-04 5.5E+00 0.0E+00 0.0E+00 1.13E-03 1.13E-03
Nicide 8 com unds H NIC 4.7E-02 3.4E+00 4.7E-02 4.1 E+02 0.0E+00 0.0E+00 8.45E-02 8.37E-02
Phosphorus Metal,Yellow or White H 7723140 5.2E-03 3.8E-01 5.3E-03 4.6E+01 0.0E+00 0.0E+00 9.46E-03 9.37E-03
POM rates,uncontrolled H POM 6.7E-04 4.9E-02 6.7E-04 5.9E+00 0.0E+00 0.0E+00 1.20E-03 1.19E-03
Selenium compounds H SEC 3.8E-04 2.8E-02 3.8E-04 3.4E+00 0.0E+00 0.0E+00 6.83E-04 8.77E-04
Toluene TH 108883 3.5E-03 2.5E-01 3.5E-03 3.0E+01 0.0E+00 0.0E+00 6.20E-03 6.20E-03
X lene 1330207 6.1E-05 4.5E-03 6.1E-05 5.3E-01 0.0E+00 0.0E+00 1.09E-04 1.09E-04
Total HAP (H) 9.2E.02 6 7E+00 8.2E-02 8.1E+02 0.0E+00 O.oE+00 1.6E-01 1.6E-M
La et HAP H 4.69E-02 3 44E+00 4.73E-02 4.15E+02 0.00E+00 0.00E+00 8.45E-02 8.37E-02
. TOXIC
EXPECTED ACTUAL EMISSIONS AFTER CONTROLS/LIMITATIONS EMISSION FACTOR
Id10' al
TOXIC AIR POLLUTANT MCASNum.
Ib/hr Ibda Ir uncontrolled controlled
Arsenic a compounds THABC 0.00E+00 0.00E+00 O.00E+00
Benzene TH 7.32E-03 1.31E-03
. . DOE+00 2.14E-04 2.14E-04
Cadium S compounds THCDC 0.00E+00 0.00E+00 O.00E+00 3.98E-04 3.94E
Fluorides sum fluoride compounds) -04
0.00E+00 O.DOE+00 0.00E+00 3.73E-02 3.73E-02
TH 000E+00 O.00E+OD O.00E+00 4.25E-02Formadeh a
Ma anese 8 eom unds TH 4.25E-02
000E+00 0.00E+00 000E+00 300E-03 2.97E-03
Mercu 8 com untie TH
HOC
0.00E-00 0.00E+00 O.00E+00 1.13E-04 1.13E-04
Methyl chloroform TH 71566 0.00E+00 0.00E+00 0.00E+00 2.36E-04 2.38E-04
Toluene TH 108883 0.00E+00 0.00E+00 0.DOE+00 I 6.20E-03 6.20E-03
Xylene (TH 1330207 1 0.00E+00 0 00E+00 0 00E+00 1 1.09E-04 1.09E-04
GREENHOUSE GAS EMISSIONS INFORMATION(FOR EMISSIONS INVENTORY PURPOSES) - GHG-POTENTIAL TO EMIT
CONSISTENT WITH EPA MANDATORY REPORTING RULE(MRR)METHOD NOT BASED ON EPA MRR METHOD
Residual Fuel Oil No.6 ACTUAL EMISSIONS POTENTIAL EMISSIONS•utilize MAX beat POTENTIAL EMISSIONS With
Input capacity and EPA MRR Emission Requested Emission Limitation-
Factors utilize requested fuel limit and EPA
GREENHOUSE GAS EPA MRR CALCULATION METHOD:TIER 1 MRR Emission Factors
POLLUTANT
short tons/yr, short tons/yr,
metric ton r metric tonstyr,CO2e short tonstyr short tons r CO2e short tonstyr CO2e
CARBON DIOXIDE(CO2) 462.73 462.73 510.07 60,915.40 60,915.40 0.00 0.00
METHANE(CH4) 1.85E-02 3.88E-01 2.04E-02 2.43E+00 5.11E+01 0.00E+00 0.00E+00
NITROUS OXIDE(N20) 3.70E-03 1.15E+00 4.08E-03 4.87E-01 1.51E+02 0.00E+00 0.00E+00
NOTE: CO2e means CO2 equivalent TOTAL .27 TOTAL TOTAL 0.00NOTE:The DAQ Air Emissions Reporting Online(AERO)system requires short tons
The EPA MRR requires metric tons

r
NATURAL GAS COMBUSTION EMISSIONS CALCULATOR REVISION H 5/24/2010-OUTPUT SCREEN
Instructions: Enter emission source/facility data on the"INPUT"tab/screen. The air emission results and summary of Input data are viewed/
printed on the"OUTPUT'tablscreen. The different tabs are on the bottom of this screen.
4 _- This spreadsheet is for your use only and should be used with caution.DENR does not guarantee the accuracy of the information contained. This
A4*01A
.- spreadsheet is subject to continual revision and updating. it is your responsibility to be aware of the most current Information available. DENR is
NCDENRnot responsible for errors or omissions that may be contained herein.
S UR E/FACILITY/USER INPUT SUMMARY ROM INPUTSCREEN)
FACILITY ID 800081
COMPANY. Perdue Farms Inc.
PERMIT NUMBER:
R: 03085T28
EMISSION SOURCE DESCRIPTION: 84 MMBTU/HR NATURAL GAS-FIRED BOILER FACILITY CITY: Lewiston
EMISSION SOURCE ID NO.: ES-8 FACILITY COUNTY: Bartle
CONTROL DEVICE: I NO CONTROL POLLUTANT CONTROL EFF.
SPREADSHEET PREPARED BY: Joe Ba ett NOX CALC'D AS 0%
ACTUAL FUEL THROUGHPUT: 233.86 10 SCF/YR FUEL HEAT VALUE: 1,020 BTU/SCF
POTENTIAL FUEL THROUGHPUT: 721.41 10 SCF/YR BOILER TYPE: SMALL BOILER <100 mmBTU/HR
REQUESTED MAX.FUEL THRPT: 0.00 10 SCF/YR NO SNCR APPLIED
CRITERIA AIR POLLUTANT EMISSIONS INFORMATION
ACTUAL EMISSIONS POTENTIAL EMSSIONS EMISSION FACTOR
(AFTER CONTROLS/EMITS) (BEFORE CONTROLS I EMITS) (AFTER CCNTROLS I UWS) Ib/mmBtu
AIR POLLUTANT EMITTED Ib/hr I tonstyr Whir tons/r Ib/hr ton r uncontrolled controlled
PARTICULATE MATTER(Total) 0.631 0.89 0.63 2.74 0.63 0.00 0.007 0.007
PARTICULATE MATTER Condensable 0.47 0.67 0.47 2.06 0.47 0.00 0.D06 0.006
PARTICULATE MATTER Filterable 0.16 0.22 0.16 0.69 0.16 0.00 0.002 0.002
SULFUR DIOXIDE S02 0.05 0.07 0.05 0.22 0.05 0.00 0.001 0.001
NITROGEN OXIDES NOx 8.24 -,11.69 8.24 36.07 8.24 0.00 0,098 0.098
CARBON MONOXIDE CO 6.92 r 9.82 6.92 30.30 6.92 0.001 0.082 0.082
VOLATILE ORGANIC COMPOUNDS(VOC) 0.45 0.84 0.45 1.98 0.45 0.00 0.005 0.005
LEAD 4.12E-05 5.8E-05 4.1E-05 1.8E-04 4.1E-05 0.0E+001 4.9E-07 4.9E-07
TOXIC/HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION
ACTUAL EMISSIONS POTENTIAL EMSSIONS EMISSION FACTOR
CAS (AFTER CONTROLS I LIMITS) (BEFORE CONTROLS I LIMITS) (AFTER CONTROLS/LIMITS) Ib/mmBtu
TOXIC I HAZARDOUS AIR POLLUTANT NUMBER Ibmr Ibst r Ib/hr lbstyr lb/hr Ibs/r uncontrolled I controlled
Arsenic&Compounds TH ASC 0.00E+00 0.00E+00 O.00E+00 0.00E+00 0.00E+00 O.00E+00 0.00E+00 0.00E+00
Benzene H 71432 1.73E-04 4.91E-01 1.73E-04 1.51E+00 1.73E-04 O.00E+00 2.06E-05 2.06E-06
Benzo a rene TH 50328 9.88E-08 2.81E-04 9.88E-08 8.66E-04 9.88E-08 O.00E+00 1.18E-09 1.18E-09
Beryllium metal H 7440417 0.00E+00 0.00E+00 O.O0E+00 0.00E+00 0.00E+00 0.00E+00 o.00E+00 0.00E+00
Cadmium&compounds H CDC O.00E+00 0.00E+00 0.00E+00 O.00E+00 0.00E+00 0.00E+00 O.00E+00 O.oOE+06
Chromium-Ali/Total H CRC 0.00E+00 O.00E+00 0.00E+00 O.00E+00 0.00E+00 O.00E+00 O.00E+00 0.00E+00
Soluble Chromate Compounds,as Chromium VI H SoICR6 0.00E+00 O.00E+00 O.o0E+00 0.00E+00 O.00E+00 O.00E+00 0.00E+00 0.00E+00
Cobalt compounds H CDC 6.92E-06 1.96E-02 6.92E-06 6.06E-02 6.92E-06 0.00E+00 e.24E-os 8.24E-08
Formaldehyde H 500DO 6.18E-03 1.75E+01 6.18E-03 5.41 E+01 6.18E-03 0.00E+00 7.35E-05 7.35E-05
Hexane n- H 110543 1.48E-01 4.21E+02 1.48E-01 1.30E+03 1.48E-01 0.00E+00 1.76E-03 1.76E-03
Manganese&compounds TH MNC 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 O.00E+00 0.00E+00 0.00E+0o
Mercury &Compounds H HGC O.00E+00 O.00E+00 O.o0E+00 0.00E+00 0.00E+00 O.00E+00 0.00E+00 0.00E+0o
Na thalene H 91203 5.02E-05 1.43E-01 5.02E-05 4.40E-01 5.02E-05 O.00E+00 5.98E-07 5.98E-07
Nickel metal TH 7440020 O.00E+00 0.00E+00 0.00E+00 O.o0E+00 0.00E+00 O.00E+00 0.00E+00 0.00E+00
Selenium compounds H SEC 1.98E-06 5.61E-03 1.98E-06 1.73E-02 1.98E-06 0.00E+00 2.35E-08 2.35E-0e
Toluene TH 108883 2.80E-04 7.95E-01 2.80E-04 2.45E+00 2.80E-04 0.00E+00 3.33E-06 3.33E-08
Total HAPs 1.55E-01 4.40E+02 I 1.55E-01 1.36E+03 I 1.55E-01 I 0.00E+00 I 1.84E-03 1.84E-03
Highest HAP JHexane 1.48E-01 I 4.21E+02 I 1.48E-01 1 1.30E+03 I 1.48E-01 I 0.00E+00 I 1.76E-03 176E-03
TOXIC AIR POLLUTANT EMISSIONS INFORMATION OR PERMITTING PURPOSES
EXPECTED ACTUAL EMISSIONS AFTER CONTROLS/LIMITATIONS EMls ib/m FACTOR
NmmB[u
TOXIC AIR POLLUTANT CAS Num. Ib/hr lb/day Ib/r uncontrolled I controlled
Arsenic&Compounds H ASC O.00E+00 0.00E+00 0.00E+00 0.00E+00 O.00E+00
Benzene TH 71432 1.73E-04 4.15E-03 O.DOE+00 20SE-061 2.0SE-oe
Benzo a rene H 50328 9.88E-08 2.37E-06 0.00E+00 1.18E-09 1.18E-09
Beryllium metal H 7440417 0.00E+00 O.00E+00 0.00E+00 0.00E+00 0.00E+00
Cadmium&compounds H CDC 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+DO
Soluble Chromate Compounds,as Chromium VI H SoICR6 O.00E+00 0.00E+00 O.00E+00 0.00E+00 o.00E+OO
Formaldehyde H 50000 6.16E-03 1.48E-01 0.00E+00 7.35E-05 7.35E-05
Hexane n- TH 110543 1.48E-01 3.56E+00 O.00E+00 1.76E-03 1.76E-03
Manganese&compounds H MNC O.00E+00 0.00E+00 O.00E+00 0.00E+0o 0.00E+0o
Mercury &Compounds H HGC 0.00E+00 O.00E+00 0.00E+00 0.00E+D0 0.00E+00
Nickel metal H 7440020 O.00E+00 0.00E+00 0.00E+00 000E+DO 0.00E+00
Toluene(TH) 108883 2.80E-04 6.72E-03 O.OOE+00 333E-06 3.33E-06
GREENHOUSE GAS EMISSIONS INFORMATION(FOR EMISSIONS INVENTORY PURPOSES) -CONSISTENT WITH EPA MANDATORY REPORTING GHG-POTENTIAL TO EMIT
RULE(MRR)METHOD NOT BASED ON EPA MRR METHOD
GREENHOUSE GAS POLLUTANT ACTUAL EMISSIONS POTENTIAL EMISSIONS
EPA MRR CALCULATION METHOD:TIER 1
metric tons/r metric tons/yr,CO2s short tonal short tons/yr short tons/yr,CO2e
CARBON DIOXIDE(CO,) 12746.44 12,746.44 14,060.52 43,005.78 43005.78
METHANE(CH4) 2.40E-01 5.05E+00 2.65E-01 8.11E-01 1.70E+01
NITROUS OXIDE(N20) 2.40E-02 7.45E+00 2.65E-02 8.11E-02 2.51E+01
TOTAL CO2e 12,768 94 TOTAL CO2e 43,047
NOTE: CO2e means CO2 equivalent metric tons Short tons

FUEL OIL COMBUSTION EMISSIONS CALCULATOR REVISION E 2/1/2010-OUTPUT SCREEN
Instructions: Enter emission source I facility data on the"INPUT"tablscreen. The air emission results and summary of Input data
are viewed I printed on the"OUTPUT'tab/screen. The different tabs are on the bottom of this screen.
This spreadsheet is for your use only and should be used with caution.DENR does not guarantee the accuracy of the Information contained.This spreadsheet
le subject to continual revision and updating.It is your responsibility to be aware of the most current Information available.DENR is not responsible for errors
NCDENR or omissions that may be contained herein.
SOURCE/PACLITY7 USER INPUT SUMMARY RO INPUT SCREEN
COMPANY: Perdue Farms Inc. MAX HEAT INPUT. 84,00 MMBTU/HR
FACILITY ID NO.: 800081 FUEL HEAT VALUE: 150,000 BTU/GAL
PERMIT NUMBER: 03085T28 HHV for GHG CALCULATIONS: 0.150 mmBTU/GAL
FACILITY CITY: Lewiston ACTUAL ANNUAL FUEL USAGE: 41,077 GAL/YR
FACILITY COUNTY: Bert a MAXIMUM ANNUAL FUEL USAGE: 4.905,600 GAL/YR
USER NAME: Joey Baggett MAXIMUM SULFUR CONTENT. 1.8 %
EMISSION SOURCE DESCRIPTION: No 6 oil fired boiler REQUESTED PERMIT LIMITATIONS
EMISSION SOURCE ID NO.: S-9 MAX.FUEL USAGE: 0 GAL/YR
MAX.SULFUR CONTENT: 1.77 %
TYPE OF CONTROL DEVICES POLLUTANT i CONTROL EFF.
SCRUBBER PM 094
NONE/OTHER S02 0.7
NONE/OTHER NOx 0
METHOD USED TO COMPUTE ACTUAL GHG EMISSIONS: TIER 1 DEFAULT HIGH HEAT VALUE AND DEFAULT EF
CARBON CONTENT USED FOR GHGS k C/al: CARBON CONTENT NOT USED FOR CALCULATION TIER CHOSEN
CRITIERIA,AIR POLLUTANT EMISSIONS INFORMATION
ACTUAL EMISSIONS POTENTIAL EMISSIONS EMISSION FACTOR
I-CONTROLS I LFITS) (BEFORE CONTROLS-TS) (AFTER CONTROLS I LafTS) Ib/103 a
AIR POLLUTANT EMITTED Whir tonslyr Ib/hr ton Iblhr tonstyr uncontrolled controlled
TOTAL PARTICULATE MATTER PM FPM+CPM 11.64 0.43 11.75 51.48 0.00 0.00 2.10E+01 2.08E+01
FILTERABLE PM(FPM) 10.81 0.40 10.91 47.80 0.00 0.00 1.95E+01 1.93E+01
CONDENSABLE PM(CPM) 0.83 0.03 0,84 3.68 0.00 0.00 1.50E+00 1.49E+00
FILTERABLE PM<10 MICRONS(PMfo) 9.36 0.34 9.45 41.37 0.00 0.00 1.69E+01 1.87E+01
FILTERABLE PM<2.5 MICRONS(PM2.e) 6.09 L5.67
6.15 26.95 0.00 0.00 1.10E+01 1.09E+01
SULFUR DIOXIDE(SO2) 154.53155.62 681.61 0.00 0.00 2.78E+02 2.76E+02
NITROGEN OXIDES(NOJ 30.8030.80 134.90 0.00 ODD 5.50E+01 5.50E+01
CARBON MONOXIDE CO 2.80 2.80 12.26 0.00 0.00 5.00E+00 5.00E+00
VOLATILE ORGANIC COMPOUNDS VOC 0.16 0.Is 069 0.00 0.00 2.80E-01 2.80E-01
LEAD 0.00 0.00 0.00 0.00 0.00 1.51E-03 1.50E-03
ACTUAL EMISSIONS POTENTIAL EMISSIONS EMISSION FACTOR
CAS (AFfeR CgITR0L8 rLMT ORE CONTROts I I-I-) (prier ccsmtots,Laar Ib/103call
TOXIC/HAZARDOUS AIR POLLUTANT NUMBER Ibfhr I r INhr lbr r Iblhr I uncontrolled controlled
Antimony&com undo H SBC 2.9E-03 '2.1E-01 2.9E-03 2.6E+01 0.0E+00 O.0E+00 5.25E-03 5.20E-03
Arsenic compounds TFI ABC 7.3E-04 5.4E-02 7.4E-04 6.5E+00 0.0E+00 0.0E+00 1.32E-03 1.31E-03
Benzene TH 71432 1.2E-04 .8.8E-03 1.2E-04 1.0E+00 0.0E+00 0.0E+00 2.14E-04 2.14E-04
Beryllium s compounds H BEC 1.5E-05 1.1E-03 1.6E-05 1.4E-01 0.0E+00 0.0E+00 2.78E-05 2.75E45
Cadium a compounds TH CDC 2.2E-04 1.6E-02 2.2E-04 2.0E+00 0.0E+00 0.0E+00 3.98E-04 3.94E-04
Chromium-AlVrotal H CRC 4.7E-04 3.4E-02 4.7E-04 4.1E+00 0.0E+00 0.0E+00 8.45E-04 8.37E-04
Cobalt compounds H COC 3.3E-03 2.4E-01 3.4E-03 3.0E+01 0.0E+00 0.0E+00 6.02E-03 5.96E-03
Eth lbenzene H IOD414 3.6E-05 2.6E-03 3.6E-05 3.1E-01 0.0E+00 0.0E+00 6.36E-05 6.36E-05
Fluorides sum fluoride compounds) 16m"88 2.1E-02 1.5E+00 2.1E-02 1.8E+02 O.0E+00 0.0E+00 3.73E-02 3.73E-02
Formaldehyde TH 50000 2.4E-02 1.7E+00 2.4E-02 2.1E+02 0.0E+00 0.0E+00 4.25E-02 4.25E-02
Lead and Lead compounds H PBC B.4E-04 6.1 E-02 8.5E-04 7.4E+00 0.0E+00 0.0E+00 1.51 E-03 1.50E-03
Manganese a compounds TH MNC 1.7E-03 1.2E-01 1.7E-03 1.5E+01 0.0E+00 0.0E+00 3.00E-03 2.97E-03
Mercurya compounds TH HGC 6.3E05 4.6E-03 6.3E-05 5.5E-01 0.0E+00 0.0E+00 1.13E-04 1.13E-04
Methyl chloroform TH 71566 1.3E-04 9.7E-03 1.3E-04 1.2E+00 0.0E+00 0.0E+00 2.36E-04 2.36E-04
Na halene H 91203 6.3E-04 4.6E-02 6.3E-04 5.5E+00 0.0E+00 0.0E+00 1.13E-03 1.13E-03
Nickle 8 compounds H NIC 4.7E-02 3.4E+00 4.7E-02 4.1 E+02 0.0E+00 0.0E+00 8.45E-02 8.37E-02
Phosphorus Metal,Yellow,or White H 7723140 5.2E-03 3.8E-01 5.3E-03 4.6E+01 0.0E+00 0.0E+00 9.46E-03 9.37E-03
ROM rates uncontrolled H POM 6.7E-04 4.9E-02 6.7E-04 5.9E+00 0.0E+00 0.0E+00 1.20E-03 1.19E-03
Selenium compounds H SEC 3.8E-04 2.8E-02 3.8E-04 3.4E+00 0.0E+Qp 0.0E+00 6.83E-04 6.77E-04
Toluene H 108883 3.5E-03 2.5E-01 3.5E-03 3.0E+01 0.0E+00 0.0E+00 6.20E-03 6.20E-03
x lene TH 1330207 6.1E-05 4.5E-03 8.1E-05 5.3E-01 0.0E+00 0.0E+00 1.09E-04 1.09E-04
Total HAP H 9.2E-02 6.7E+00 9.2E-02 8.1E+02 0.0E+00 0.0E+00 1.6E-01 1.6E-01
La et HAP H 4.69E-02 3.44E+00 4 73E-02 4.15E+02 0.00E+00 0.00E+00 8.45E-02 8.37E-02
EXPECTED ACTUAL EMISSIONS AFTER CONTROLS I LIMITATIONS EMISSION FACTOR
1 10' al
TOXIC AIR POLLUTANT CAS Num. Ib/hr lb/day lblyr uncontrolled controlled
Arsenic a com unds TH ASC 0.00E+00 0.00E+00 0.00E+00 1.32E-03 1.31E-03
benzene TH 71432 0.00E+00 0.00E+00 0.00E+00 214E-04 2.14E-04
Cadium a compounds TH CDC 0.00E+00 0.00E+00 O.00E+00 3.98E-04 3.94E-04
Fluordes sum fluoride compounds) T 16984488 O.00E+00 0.00E+00 O.o0E+00 3.73E-02 3.73E-02
Formaldehyde TH 50000 0.00E+00 0.00E+00 0.00E+00 4.25E-02 4.25E-02
Manganese d compounds TH MNC O.00E+00 0.00E+00 0.00E+00 3.00E-03 2.97E-03
Mercury d compounds TH HGC 0.00E+00 0.00E+00 0.00E+00 1.13E-04 1.13E-04
MeM I chloroform TH 71566 0.00E+00 0.00E+00 0.00E+00 2 36E-04 2.38E-04
Toluene TH 108883 0.00E+00 0.00E+00 0.00E+00 6 20E-03 6.20E-03
Xylene (TH) 1330207 0.00E+00 000E+00 0.00E+00 109E-04 1 09E-44
GREENHOUSE GAS EMISSIONS INFORMATION(FOR EMISSIONS INVENTORY PURPOSES) - GHG-POTENTIAL TO EMIT
CONSISTENT MTH EPA MANDATORY REPORTING RULE(MRR)METHOD NOT BASED ON EPA MRR METHOD
Residua/Fuel Oil No.6 ACTUAL EMISSIONS POTENTIAL EMISSIONS-udlize Max heat POTENTIAL EMISSIONS With
Input capacity and EPA MRR Emission Requested Emission Limitation-
Factors utilize requested fuel limit and EPA
GREENHOUSE GAS EPA MRR CALCULATION METHOD:TIER 1 MRR Emission Factors
POLLUTANT short tons/yr, short tons/yr,
metric ton r metric ton r,CO2e short ton r short tons/ r CO2e short ton r CO2e
CARBON DIOXIDE(CO2) 462.73 462.73 510.07 60,915.40 60,915.40 0.00 0.00
METHANE(CH4) 1.85E-02 3.88E-01 2.04E-02 2.43E+00 5.11E+01 O.00E+00 0.00E+00
NITROUS OXIDE(N20) 3.70E-03 1.15E+00 4.08E-03 4.87E-01 1.51E+02 0.00E+00 0.00E+00
TOTAL TOTAL TOTAL 0.00
NOTE: CO2e means CO2 equivalent
NOTE:The DAQ Air Emissions Reporting Online(AERO)system requires short tons
The EPA MRR requires metric tons

NATURAL GAS COMBUSTION EMISSIONS CALCULATOR REVISION H 5/24/2010-OUTPUT SCREEN
A,
Instructions: Enter emission source I facility data on the"INPUT"tab/screen. The air emission r.suits and summary of Input data are viewed/
printed on the"OUTPUT"tab/screen. The different tabs are on the bottom of this screen.
This spreadsheet Is for your use only and should be used with caution.DENR does not guarantee the accuracy of the information contained. This
NCDENR spreadsheet is subject to continual revision and updating. It is your responsibility to be aware of the most current information available. DENR Is
not responsible for errors or omissions that may be contained herein.
SO UR E/FA CIL ITY/USER INPUT SUMMARY FROM/NPUT REEN
COMPANY. Perdue Farms inc. FACILITY ID NO.. 800081
PERMIT NUMBER: 03O85T28
EMISSION SOURCE DESCRIPTION: 84 MMBTU/HR NATURAL GAS-FIRED BOILER FACILITY CITY: Lewiston
EMISSION SOURCE ID NO.: ES-9 FACILITY COUNTY: Bertie
CONTROL DEVICE: I NO CONTROL POLLUTANT I CONTROL EFF.
SPREADSHEET PREPARED BY: Joey Baggett
ACTUAL FUEL THROUGHPUT: 233.86 �MNCSNCRAPPLIED
FUEL HEAT VALUE: 1,020 BTU/SCF NOX CALC'D AS 0%
POTENTIAL FUEL THROUGHPUT: 721.41 BOILER TYPE: SMALL BOILER <100 mmBTU/HR
REQUESTED MAX.FUEL THRPT: 0.00
CRITERIA AIR POLL EMISSIONS INFORMATION
ACTUAL EMISSIONS POTENTIAL EMSSIONS EMISSION FACTOR
(AFTERCONTRMSILMNTS) (BEFORE CONrROLb/UWTS) (AFTER CONTROLS I UMnS) Ib/mmStu
AIR POLLUTANT EMITTED Ib/hr tonslyr Whir tonslyr Ib/hr tons/r uncontrolled controlled
PARTICULATE MATTER Total 0.63 0.89 0.63 2.74 0.63 0.00 0.007 0.007
PARTICULATE MATTER Condensable 0.47 0.67 0.47 2.06 0.47 0.00 0.D06 0.006
PARTICULATE MATTER Filterable 0.16 0.22 0.16 0.69 0.16 0.00 0.002 0.002
SULFUR DIOXIDE S02 0.05 ' 0.07 0.05 0.22 0.05 0.00 0.001 0.001
NITROGEN OXIDES NOx 8.24 11.69 8.24 36.07 8.24 0.00 0.098 0.098
CARBON MONOXIDE CO 6.92 9.82 6.92 30.30 6.92 0.00 0.082 0.082
VOLATILE ORGANIC COMPOUNDS VOC 0.45 0.64 0.45 1.98 0.45 0.00 0.005 0.005
LEAD 4.12E-OS 5.8E-05 4.1E-05 1.8E-04 4.1E-05 0.0E+00 4.9E-07 4.9E-07
TOXIC/HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION
ACTUAL EMISSIONS POIENTIAL EMSSIONS EMISSION FACTOR
CAS (11 R CONTRMS I LIMITS) (BEFORE CO TRMS I LIMITS) (AFTER CCNTRMS I LIMITS) Ib/mmBtu
TOXIC I HAZARDOUS AIR POLLUTANT NUMBER Ib1hr Ibs/r Ib/hr Ibs/ Iblllr lbtyr uncontrolled controlled
Arsenic&Compounds TH ASC O.00E+00 0.00E+00 O.00E+00 O.00E+00 O.00E+00 O.00E+00 o.DOE+00 0.o0E+00
Benzene TH 71432 1.73E-04 -4.91E-01 1.73E-04 1.51E+00 1.73E-04 O.00E+00 2.06E-06 2.06E-06
Benzo a rene TH 50328 9.88E-08 2.81E-04 9.88E-08 8.66E-04 9.88E-08 0.00E+00 1 16E-09 1.18E-09
Beryllium metal TH 7440417 0.00E+00 O.00E+00 0.00E+00 0.00E+00 0.00E+00 O.00E+00 0 00E+00 0.00E+00
Cadmium&compounds H CDC O.00E+00 O.00E+00 0 00E+00 O.00E+00 0.00E+00 O.00E+00 0.00E+00 O.00E+00
Chromium-AIUTotal H CRC 0.00E+00 O.00E+00 O.00E+00 O.00E+00 O.00E+00 O.00E+00 0.00E+0o O.DOE+00
Soluble Chromate Compounds,as Chromium VI TH SoICR6 O.00E+00 O.00E+00 O.00E+DO O.00E+00 O.00E+00 O.00E+00 O.00E+00 0.00E+00
Cobalt compounds H CDC 6.92E-06 1.96E-02 6.92E-06 6.06E-02 6.92E-06 O.00E+00 8.24E-08 9.24E-08
Formaldehyde TH 50000 6.18E-03 9.75E+01 6.18E-03 5.41E+01 6.18E-03 O.00E+00 7.35E-05 7.35E-05
Hexane,n- TH 110543 1.48E-M 4.21E+02 1.48E-01 1.30E+03 1.48E-01 0.00E+00 1.76E-03 1.76E-03
Manganese&compounds H MNC O.00E+00 O.00E+00 O.00E+00 O.00E+00 O.00E+00 0.00E+00 0.00E+00 0.00E+00
Mercury &Compounds TH HGC O.00E+00 0.00E+00 0.00E+00 O.00E+DO O.00E+00- D.00E+00 0.00E+00 0.00E+00
Na thalene H 91203 5.02E-05 1.43E-01 5.02E-05 4.40E-01 5.02E-05 O.00E+00 5.98E-07 5.98E-07
Nickel metal TH 7440020 0.00E+00 00E 0.00E+00 0.00E+ 0 0.00E+00 0..00E00 o.00ewo 0.80E+oo
+
61 +00
Selenium compounds H SEC 1.98E-06 5E13 E-0 2.35E-06 2.35E-06
Toluene TH 108883 2.80E-04 7.95E-01 -04 2.45E+00 2.80E-04 000E
3.33E 06 3.33E-06
Total HAPs 1.55E-01 4.40E+02 I 1.55E-01 1.36E+03 1.55E-01 10.00E+00 I 1.64E-03 1.94E-03
Highest HAP IHexane 1.48E-01 4.21E+02 I 1.48E-01 I 1.30E+03 1 1.48E-01 I O.ODE+00 I 1.76E-03 176E-03
TOXIC AIR POLLUTANT EMISSIONS INFORMATION OR PERMITTING PURPOSES
EXPECTED ACTUAL EMISSIONS AFTER CONTROLS/LIMITATIONS EMISSION FACTOR
Ib/mmBtu
TOXIC AIR POLLUTANT CAS Num. Ib/hr lb/day ib/r uncontrolled controlled
Arsenic&Compounds TH ASC O.00E+00 O.00E+00 O.00E+00 O.00E+00 O.00E+00
Benzene TH 71432 1.73E-04 4.15E-03 O.00E+00 2.o6E-06 2.06E-08
Benzo a rene TH 50328 9.88E-08 2.37E-06 0.00E+00 1.18E-09 1A E-o9
Beryllium metal TH 7440417 O.00E+00 O.00E+00 0.00E+00 0.00E+0o O.00E+00
Cadmium&compounds H CDC O.00E+00 0.00E+00 0.00E+00 O.00E+00 0.00E+00
Soluble Chromate Compounds,as Chromium I H SoICR6 0.00E+00 O.00E+00 O.00E+00 o.00E+00 0.00E+00
Formaldehyde TH 50000 6.18E-03 1.48E-01 O.ODE+00 7.35E-05 7.35E-05
Hexane n- TH 110543 1.48E-01 3.56E+00 O.00E+00 1.76E-03 1.76E-03
Man anese&compounds H MNC O.ODE+00 0.00E+00 O.00E+00 0.00E+00 0.00E+00
Mercury &Compounds H HGC O.00E+00 O.00E+00 O.00E+00 0.00E+00 O.00E+00
Nickel metal H 7440020 0.00E+00 0.00E+00 O.00E+00 OoOE+00 000E+00
Toluene TH) 108883 2.80E-04 6.72E-03 0.00E+00 333E_rI 3.33E-06
GREENHOUSE GAS EMISSIONS INFORMATION(FOR EMISSIONS INVENTORY PURPOSES) -CONSISTENT N9TH EPA MANDATORY REPORTING GHG-POTENTIAL TO EMIT
RULE(MRR)METHOD NOT BASED ON EPA MRR METHOD
GREENHOUSE GAS POLLUTANT ACTUAL EMISSIONS POTENTIAL EMISSIONS
EPA MRR CALCULATION METHOD:TIER 1
metric tons/yr metric tons/yr,CO2e short tonslyr short tonsfyr short tons/yr,CO2e
CARBON DIOXIDE(CO2) 12746.44 12,746.44 1 14,050.52 43,005.78 43005.78
METHANE(CH4) 2.40E-01 5.05E+00 2.65E-01 8.11E-01 1.70E+01
NITROUS OXIDE(N20) 2.40E-02 7 45E+00 2.65E-02 8.11E-02 2.51E+01
TOTAL CO2e 12,788% TOTAL CO2e 1147 86
NOTE: CO2e means CO2 equivalent metric tons) short tons

NATURAL GAS COMBUSTION EMISSIONS CALCULATOR REVISION H 5/24/2010-OUTPUT SCREEN
Instructions: Enter emission source I facility data on the"INPUT"tab/screen. The air emission results and summary of input data are viewed/
printed on the"OUTPUT"tab/screen. The different tabs are on the bottom of this screen.
le
This spreadsheet is for your use only and should be used with caution.DENR does not guarantee the accuracy of the information contained. This
NCDENR spreadsheet is subject to continual revision and updating. It is your responsibility to be aware of the most current information available. DENR Is
not responsible for errors or omissions that may be contained herein.
SOURCE/FA ILITY/USER INPUT SUMMARY FROM INPUT SCREEN
COMPANY. Perdue Farms Inc. FACILITY ID NO.: 800081
__ PERMIT NUMBER: 03085T28
EMISSION SOURCE DESCRIPTION: 89 MMBTU/HR NATURAL GAS-FIRED BOILER FACILITY CITY: Lewiston
EMISSION SOURCE ID NO.: ES-23 FACILITY COUNTY: Bertie
CONTROL DETIC-E- 1 LOW NOx BURNERS POLLUTANT CO�NTROL EFF.
SPREADSHEET PREPARED BY: Joey Baggett
ACTUAL FUEL THROUGHPUT: 58.30 10 SCF/YR FUEL HEAT VALUE: 1,020 BTU/SCF NOX CALC'D AS 50%
POTENTIAL FUEL THROUGHPUT: 764.35 1 CIP SCF/YR I BOILER TYPE: SMALL BOILER <100 mmBTU/HR
REQUESTED MAX.FUEL THRPT: 0.00 10 SCF/YR NO SNCR APPLIED
CRITERIA AIR POLLUTANT EMISSIONS INFORMATION
ACTUAL EMISSIONS POTENTIAL EMSSIONS EMISSION FACTOR
(AFTER CONTROLS I UMRS) (SEFORE CONTROLS I UMRS) (AFTER CONTROLS I UMTS) Ib/mmBtu
AIR POLLUTANT EMITTED Ib/hr tons/r Ib/hr ton r Ib/hr tonslyr uncontrolled Iwntrolled
PARTICULATE MATTER Total 0.66 0.22 0.66 2.90 0.66 0.00 0.0071 0.007
PARTICULATE MATTER Condensable 0.50 0.17 0.50 2.18 0.50 0.00 0.006 0.006
PARTICULATE MATTER Filterable 0.17 0.06 0.17 0.73 0.17 0.00 0.002 0.002
SULFUR DIOXIDE S02 0.05 0.02 0.05 0.23 0.05 0.00 0.001 0.001
NITROGEN OXIDES NOx 4.36 1.46 8.73 38.22 4.36 0.00 0.098 0.049
CARBON MONOXIDE CO 7.33 2.45 7.33 32.10 7.33 0.00 0.082 0.082
VOLATILE ORGANIC COMPOUNDS VOC 0.48 0.16 0.48 2.10 0.48 0.00 0.005 0.005
LEAD 4.36E-05 1.5E-05 4.4E-05 1.9E-04 4.4E-05 0.0E+00 4.9E-07 4.9E-07
TOXIC/HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION
ACTUAL EMISSIONS POTENTIAL EMSSIONS EMISSION FACTOR
CAS (AFTERCONTROLSIUMITS) (6EFORECO TROLS I UMITS) (AFTER CONTROLS I OMITS) Ib/mmBtu
TOXIC I HAZARDOUS AIR POLLUTANT NUMBER Ib/hr Ib6/r INhr IbWyr Ib/hr Ibstyr uncontrolled controlled
Arsenic&Compounds H ASC 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.o0E+00 0.(10E+00
Benzene TH 71432 1.83E-04 1.22E-01 1.83E-04 1.61E+00 1.83E-04 0.00E+00 2oSE-06 2.06E-M
Benzo a rene H 50328 1.05E-07 7.00E-05 1.05E-07 9.17E-04 1.05E-07 0.00E+00 1.18E-09 1.18E-09
Beryllium metal TH 7440417 O.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 O.00E+00 0.00E+00
Cadmium&compounds H CDC 0.00E+00 0.00E+00 0.00E+OD O.DOE+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00
Chromium-AII/Total H CRC 0.00E+00 O.00E+00 0.00E+00 O.DOE+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00
Soluble Chromate Compounds,as Chromium I H SoICR6 O.o0E+00 0.00E+00 0.00E+00 O.00E+00 O.00E+00 0.00E+00 0.00E+00 0.00E+00
Cobalt compounds H COG 7.33E-06 4.90E-03 7.33E-06 I 6.42E-02 7.33E-06 0.00E+00 8.24E-08 8.24E-0e
Formaldehyde H 50000 6.54E-03 4.37E+00 6.54E-03 5.73E+01 6.64E-03 O.00E+00 7.35E-05 7.35E-05
Hexane,n- TH 110543 1.57E-01 1.05E+02 1.57E-01 1.38E+03 1.57E-01 0.00E+00 1.76E-03 1.76E-03
Manganese&compounds H MNC O.00E+00 O.00E+00 O.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00
Mercury &Compounds H HGC 0.00E+00 D.00E+00 0.00E+00 0.00E+00 O.00E+00 0.00E+00 0.00E+00 0.o0E+00
Na thalene H 91203 5.32E-05 3.56E-02 5.32E-05 4.66E-01 5.32E-05 0.00E+00 5.98E-07 5.99E-07
Nickel metal H 7440020 1 0.00E+00 0.00E+00 0.00E+00 O.00E+00 0.00E+00 O.00E+00 0.00E+00 0.00E+00
Selenium compounds H SEC I 2.09E-06 I 1.40E-03 2.09E-06 1.83E-02 2.09E-05 0.00E+00 2.35E-08 2.35E-08
Toluene TH 108883 1 2.97E-04 I 1.98E-01 2.97E-04 2.60E+00 2.97E-04 I O.DOE+00 3.33E-06 3.33E-06
Total HAPs 1.64E-01 1 1.10E+02 I 1.64E-01 I 1.44E+03 1 64E-01 O.00E+00 164E-03 1.64E-03
Highest HAP Hexane 1.57E-01 1.05E+02 1.57E-01 1.38E+03 1.57E-01 0.00E+00 1.76E-03 1 76E-03
TOXIC AIR POLLUTANT EMISSIONS INFORMATION OR PERMITTING PURPOSES
EXPECTED ACTUAL EMISSIONS AFTER CONTROLS I LIMITATIONS EMISSION FACTOR
W-0tu
TOXIC AIR POLLUTANT CAS Num. Ib/hr lb/day Ib/r uncontrolled controlled
Arsenic&Compounds TH ASC 0.00E+00 O.00E+00 0.00E+00 0.00E+00 o.00E+00
Benzene TH 71432 1.83E-04 4.40E-03 0.00E+00 2.06E-06 2.06E-06
Benzo a rene H 50328 1.05E-07 2.51E-06 O.00E+00 1.18E-09 1.1eE-09
Beryllium metal H 7440417 O.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00
Cadmium&compounds TH CDC O.DOE+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00
Soluble Chromate Compounds,as Chromium I H SoICR6 0.00E+00 0.00E+00 O.00E+00 0.00E+00 O.00E+00
Formaldehyde H 50000 6.54E-03 1.57E-01 O.00E+00 7.35E-05 7.35E-05
Hexane n- H 110543 1.57E-01 3.77E+00 O.00E+00 1.76E-03 1.76E-03
Manganese&compounds TH MNC 0.00E+00 O.00E+00 0.00E+00 0.00E+00 0.00E+00
Mercury &Compounds H HGC O.00E+OO O.00E+00 0.00E+00 0.00E+00 0.00E+00
Nickel metal TH 7440020 0.00E+00 0.00E+00 0.00E+00 0.00E+Oo 0.00E+oo
Toluene(TH 108883 2.97E-04 7.12E-03 0.00E+00 3 33E-06 3 33E-06
GREENHOUSE GAS EMISSIONS INFORMATION(FOR EMISSIONS INVENTORY PURPOSES) -CONSISTENT WITH EPA MANDATORY REPORTING GHG-POTENTIAL TO EMIT
RULE(MRR)METHOD NOT BASED ON EPA MRR METHOD
GREENHOUSE GAS POLLUTANT ACTUAL EMISSIONS POTENTIAL EMISSIONS
EPA MRR CALCULATION METHOD:TIER 1
metric ton r metric tons/yr,CO29 short tonstyr short tonstyr short tons/yr,CO2e
CARBON DIOXIDE(CO2) 3177.62 3,177.62 3.502.72 45,565.65 45565.65
METHANE(CH4) 5.99E-02 1.26E+00 6.61E-02 8.59E-01 1.80E+01
NITROUS OXIDE(N20) 5.99E-03 1.86E+00 6.61E-03 8.59E-02 2.66E+01
TOTAL CO2e 1 3,180.73 TOTAL CO2e 46 610.34
NOTE: CO2e means CO2 equivalent metric tons) short tons

LIQUEFIED PETROLUEM GAS(LPG)COMBUSTION EMISSIONS CALCULATOR-REVISION D 2/1/2010-OUTPUT SCREEN
Instructions: Enter emission source I facility data on the"INPUT tab/screen. The air emission results and summary of input
MA data are viewed/printed on the"OUTPUT'tab/screen. The different tabs are on the bottom of this screen.
7AJ A. This spreadsheet is for your use only and should be used with caution.DENR does not guarantee the accuracy of the information
NCDENR contained. This spreadsheet is subject to continual revision and updating. It is your responsibility to be aware of the most
current information available. DENR is not responsible for errors or omissions that may be contained herein.
INPUT
COMPANY: Perdue Farms Inc. FACILITY ID NO.: 800081
PERMIT NUMBER: 03085T28
EMISSION SOURCE DESCRIPTION: 4.4 MMBTU/HR FIRED BOILER FACILITY CITY: Lewiston
EMISSION SOURCE ID NO.: es-6,7 FACILITY COUNTY: Bertie
SPREADSHEET PREPARED BY: Joey Baggett LPG Make U %
ACTUAL FUEL THROUGHPUT: 176,982 GAWR FUEL HEAT VALUE: 91,000 BTU/Gal Propane: 1 96.80
POTENTIAL FUEL THROUGHPUT: 301,714 GAWR HHV USED FOR GHGs: 0.092 mm BTU/Gal Butane: 3.20
REQUESTED MAX.FUEL THRPT: 0 GAWR BOILER TYPE: COMMERCIAL
METHOD USED TO COMPUTE ACTUAL GHG EMISSIONS: TIER 1: DEFAULT HIGH HEAT VALUE AND DEFAULT EF
CARBON CONTENT USED FOR GHGS k C/ al: CARBON CONTENT NOT USED FOR CALCULATION TIER CHOSEN
CRITERIA AIR POLLUTANT EMISSIONS INFORMA7ION
ACTUAL EMISSIONS POTENTIAL EMSSIONS EMISSION FACTOR
(AFTER CONTROLS I LIMITS) (BEFORE CONTROLS I LIMITS) (AFTERCONTROLS/LIMITS) Ib/mmBtu
AIR POLLUTANT EMITTED Ib/hr tons/r Ib/hr tons/ Ib/hr tons r uncontrolled controlled
PARTICULATE MATTER PM 0.03 0.06 0.03 0.15 0.03 0.00 0.008 0.008
PARTICULATE MATTER<10 MICRONS(PM(o) 0.03 0.06 0.03 0.15 0.03 0.00 0.008 0.008
PARTICULATE MATTER<2.5 MICRONS(PM2.5) 0.03 0.06 0.03 0.15 0.03 0.00 0.008 0.008
SULFUR DIOXIDE S02 0.00 0.00 0.00 0.00 0.00 0.00 1.63E-04 1.63E-04
NITROGEN OXIDES NOx 0.63 1.15 0.63 2.74 0.63 0.00 0.142 0.142
CARBON MONOXIDE CO 0.36 0.66 0.36 1.58 0.36 0.00 0.082 0.082
VOLATILE ORGANIC COMPOUNDS VOC 0.05 0.09 0.05 0.21 0.05 0.00 (.011 0.011
TOXIC/HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION
ACTUAL EMISSIONS POTENTIAL EMSSIONS EMISSION FACTOR
CAS (AFTER CONTROLS I LIMITS) (BEFORE CONTROLS I LIMITS) (AFTER CONTROLS I LIMITS) Ib/mmBtu
TOXIC I HAZARDOUS AIR POLLUTANT NUMBER Ib/hr tons r Ib/hr ton Ib/hr tons/r uncontrolled controlled
TOXIC AIR POLLUTANT EMISSIONS INFORMATION ffo PERMITTING PURPOSES
EXPECTED ACTUAL EMISSIONS AFTER CONTROLS 1 LIMITATIONS EMISSION FACTOR
Ib/mmBtu
TOXIC AIR POLLUTANT ICAS Num. I Ib/hr IbIday b uncontrolled controlled
GREENHOUSE GAS POLLUTANT EMISSIONS INFORMATION(FOR EMISSION INVENTORY GHG-POTENTIAL TO EMIT
PURPOSES) NOT BASED ON EPA MRR METHOD
ACTUAL EMISSIONS POTENTIAL EMISSIONS With Requested
LPG POTENTIAL EMISSIONS-utilize max heat input Emission Limitation-utilize requested fuel
EPA MRR CALCULATION METHOD: TIER 1 capacity and EPA MRR Emission Factors limit and EPA MRR Emission Factors
GREENHOUSE GAS
EMITTED metric tons/yr metric tons/r,CO2e short tons/r short tons/r short tons/r,CO2e short tons/r short tons/r,CO2e
CARBON DIOXIDE(CO2) 1,025.46 1,025.46 1,130.38 2,675.86 2,675.86 0.00 0.00
METHANE(CH4) 4.88E-02 1.03E+00 5.38E-02 1.27E-01 2.68E+00 0.00E+00 0.00E+00
NITROUS OXIDE(N20) 9.77E-03 3.03E+00 1.08E-02 2.55E-02 7.90E+00 0.00E+00 O.00E+00
TOTAL 1,029.52 TOTAL 2,686.44 TOTAL 0.00
NOTE: CO2e means CO2 equivalent.
NOTE: The DAQ Air Emissions Reporting Online(AERO)system requires short tons be reported. The EPA MRR requires metric tons be reported.

Large Diesel and All Dual-Fuel Engines Emissions Calculator LGD2009 Revision A
Instructions:Please provide the information shown in blue below.The applicability of this spreadsheet is limited to diesel engines larger than 600 hp and all dual-fuel(diesel/natural gas)engines.Please note
that,when used in conjunction with permit applications,any value entered for annual operations of these engines may become a permit limit.
For annual emissions enter either:(1)Annual Electrical Output,(2)Engine Output and Annual Operation(leave the formula for calculating Annual Electrical Output unchanged)or
(3)Generator Output(kW)and Annual Operation(remember to copy the resulting Annual Electrical Output to the appropriate cell to the left).
User Input This section can be used to calculate kW-hr output DISCLAIMER:This spreadsheet is for your use only and
Company Name: Perdue Farms Incorporated from hours of operation and engine hp output. should be used with caution.DENR does not guarantee the
Plant County: Bertie This can be useful for operators with hour meters but accuracy of the information contained. This spreadsheet is
Plant City: Lewiston no Waft-hour meters.It assumes full load operation subject to continual revision and updating. It is your
Permit Number: 03085T28 resulting in conservative emission estimates. responsibility to be aware of the most current information
User:
ES-22A available. DENR is not responsible for errors or omissions
Diesel Fuel Sulfur Content(%): 0.05 Annual Operation(hours): 128 that may be contained herein.
NG Fuel Sulfur Content(gr/mm cu ft): 2,000
Engine Output(hp): 2628 Generator Output(kW): 1825
Annual Electrical Output(kW-hr): 220,741 Annual Output(kW-hr): 233,600
Annual Output h -hr: 1 336,384 <-----Copy results to"Annual Output kW-hr"at left if desired.
Emissions Output for Diesel Engines Emission Factor Emissions Output for Dual-fuel Engines Emission Factor
Criteria Pollutants Factor Quality Criteria Pollutants Factor Quality
Pollutant Ib/hr Ib/ r t Ib/h hr Rating Pollutant Ib/hr Ib/ r t Ib/h hr Rating
PM 1.8E+00 2.4E+02 1.2E-01 7.00E-04 B PM NA NA NA NO NA
PM-10 1.8E+00 2.4E+02 1.2E-01 7.00E-04 B PM-10 NA NA NA NO NA
PM-2.5 1.8E+00 2.4E+02 1.2E-01 7.00E-04 B PM-2.5 NA NA NA NO NA
NO,uncont. 6.3E+01 8.1 E+03 4.0E+00 2.40E-02 B NO,uncont. 4.7E+01 6.1 E+03 3.0E+00 1.80E-02 D
NO.,cont. 3.4E+01 4.4E+03 2.2E+00 1.30E-02 B NO.,cont. NA NA NA NO NA
TOC(as CH4) 1.9E+00 2.4E+02 1.2E-01 7.05E-04 C TOC(as CH4) 1.4E+01 1.8E+03 8.9E-01 5.29E-03 D
NMTOC 1.7E+00 2.2E+02 1.1 E-01 6.42E-04 E NMTOC 3.5E+00 4.4E+02 2.2E-01 1.32E-03 E
CO 1.4E+01 1.9E+03 9.3E-01 5.50E-03 C CO 2.0E+01 2.5E+03 1.3E+00 7.50E-03 D
sox 1.1E+00 1.4E+02 6.8E-02 4.05E-04 B SOx 5.5E-02 7.0E+00 3.5E-03 2.09E-051 B
Total HAP 3.1E-02 4.0E+00 2.0E-03 1.19E-05
Largest HAP 1.4E-02 1.8E+00 9.1 E-04 5.43E-06
Toxic/Hazardous Air Pollutants There are no Toxic/Hazardous Air Pollutant emission factors for dual-fuel engines.
Pollutant Ib/hr lb/day Ib! r
Acetaldehyde 4.6E-04 NA 5.9E-02 1.76E-07 E
Acrolein 1.4E-04 NA 1.9E-02 5.52E-08 E
Benzene 1.4E-02 NA 1.8E+00 5.43E-06 E
Benzo(a)pyrene 4.7E-06 NA 6.1 E-04 1.80E-09 E,<
Formaldehyde 1.5E-03 NA 1.9E-01 5.52E-07 E
Napthalene 2.4E-03 NA 3.1E-01 9.10E-07 E
Total PAH 3.9E-03 NA 5.0E-01 1.48E-06 E,<
Toluene 5.2E-03 1.2E-01 6.6E-01 1.97E-06 E
X lenes 3.6E-03 8.5E-02 4.5E-01 1.35E-06 E
NO,control is via ignition timing retard.
Emission Factor Emission Factor
Greenhouse Gases Factor Quality Greenhouse Gases Factor Quality
Pollutant Ib/ r t Ib/h hr Rating rNitrous
Ib/hr Ib/ r t Ib/h hr Rating
Carbon Dioxide(COz) 3.8E+05 1.9E+02 0.31 NA xide(COz) 2.8E+05 1.4E+02 0.23 NA
Methane(CH4) 2.1 E+01 1.1 E-02 0.0001 NA H4) 1.3E+03 6.4E-01 0.004 NA
Nitrous Oxide(N20) 3.1 E+00 1.6E-03 0.00001 NA e(N20) 3.1 E+00 1.6E-03 0.00001 NA
LGD2008 Revision A dated June 30,2008
Pollutants in red are federally regulated hazardous air pollutants(HAPs)only. All other toxic/hazardous air pollutants are regulated as both HAPs and TAPs.
Factor quality ratings containing"<"indicate an AP-42 emission factor based on test results being below detection.
Emission factors for criteria and toxic/hazardous pollutants are from AP-42 Chapter 3.4,Large Stationary Diesel and All Stationary Dual-fuel Engines,dated October 1996.
Emission factors for greenhouse gases are from DAQ's Greenhouse Gas Emission Guidelines:Stationary Combustion Sources,June 2008,except for CH4,
which uses AP-42,Chapter 3.4,Large Stationary Diesel and All Stationary Dual-fuel Engines,dated October 1996. NCDENR
Carbon dioxide emission factor for dual-fuel engines is calculated based on 95%natural gas and 5%diesel,per AP-42 Section 3.4,p.3.4-5,revised 10/96.
Hourly emission rates for all pollutants are based on the hourly engine output.Annual emissions are based on the annual engine output.
Daily emissions are based on operation at the hourly output rate for 24 hours.

Large Diesel and All Dual-Fuel Engines Emissions Calculator LGD2009 Revision A
Instructions:Please provide the information shown in blue below.The applicability of this spreadsheet is limited to diesel engines larger than 600 hp and all dual-fuel(diesel/natural gas)engines.Please note
that,when used in conjunction with permit applications,any value entered for annual operations of these engines may become a permit limit.
For annual emissions enter either:(1)Annual Electrical Output,(2)Engine Output and Annual Operation(leave the formula for calculating Annual Electrical Output unchanged)or
(3)Generator Output k and Annual Operation(remember to copy the resulting Annual Electrical Output to the appropriate cell to the left).
User Input This section can be used to calculate kW-hr output DISCLAIMER:This spreadsheet is for your use only and
Company Name: Perdue Farms Incorporated from hours of operation and engine hp output. should be used with caution.DENR does not guarantee the
Plant County: Bertie This can be useful for operators with hour meters but accuracy of the information contained. This spreadsheet is
Plant City: Lewiston no Waft-hour meters.It assumes full load operation subject to continual revision and updating. It is your
Permit Number: 03085T28 resulting in conservative emission estimates. responsibility to be aware of the most current information
User: ES-22B
available. DENR is not responsible for errors or omissions Diesel Fuel Sulfur Content(%): 0.05 Annual Operation(hours): 127 that may be contained herein.
NG Fuel Sulfur Content(gr/mm cu ft): 2,000
Engine Output(hp): 2628 Generator Output(kW): 1825
Annual Electrical Output(kW-hr): 219,016 Annual Output(kW-hr): 231,775
Annual Output h -hr: 1 333,756 <-----Copy results to"Annual Out ut kW-hr"at left if desired.
Emissions Output for Diesel Engines Emission Factor Emissions Output for Dual-fuel Engines Emission Factor
Criteria Pollutants Factor Quality Criteria Pollutants Factor Quality
Pollutant Ib/hr Ib/ r t Ib/h hr Rating Pollutant Ib/hr Ib! r t Ib/h -hr Rating
PM 1.8E+00 2.3E+02 1.2E-01 7.00E-04 B PM NA NA NA ND NA
PM-10 1.8E+00 2.3E+02 1.2E-01 7.00E-04 B PM-10 NA NA NA ND NA
PM-2.5 1.8E+00 2.3E+02 1.2E-01 7.00E-04 B PM-2.5 NA NA NA ND NA
NO.,uncont. 6.3E+01 8.0E+03 4.0E+00 2.40E-02 B NO.,uncont. 4.7E+01 6.0E+03 3.0E+00 1.80E-02 D
NO..cont. 3.4E+01 4.3E+03 2.2E+00 1.30E-02 B NO.,cont. NA NA NA NO NA
TOC(as CH4) 1.9E+00 2.4E+02 1.2E-01 7.05E-04 C TOC(as CH4) 1.4E+01 1.8E+03 8.8E-01 5.29E-03 D
NMTOC 1.7E+00 2.1E+02 1.1E-01 6.42E-04 E NMTOC 3.5E+00 4.4E+02 2.2E-01 1.32E-03 E
CO 1.4E+01 1.8E+03 9.2E-01 5.50E-03 C CO 2.0E+01 2.5E+03 1.3E+00 7.50E-03 D
SO„ 1.1E+00 1.4E+02 6.8E-02 4.05E-04 B sox 5.5E-02 7.0E+00 3.5E-03 2.09E-051 B
Total HAP 3.1E-02 4.0E+00 2.0E-03 1.19E-05
Largest HAP I 1.4E-02 1.8E+00 9.1E-04 5.43E-06
Toxic/Hazardous Air Pollutants There are no Toxic/Hazardous Air Pollutant emission factors for dual-fuel engines.
Pollutant Ib/hr lb/day Ib/ r
Acetaldehyde 4.6E-04 NA 5.9E-02 1.76E-07 E
Acrolein 1.4E-04 NA 1.8E-02 5.52E-08 E
Benzene 1.4E-02 NA 1.8E+00 5.43E-06 E
Benzo(a)pyrene 4.7E-06 NA 6.0E-04 1.80E-09 E,<
Formaldehyde 1.5E-03 NA 1.8E-01 5.52E-07 E
Napthalene 2.4E-03 NA 3.0E-01 9.10E-07 E
Total PAH 3.9E-03 NA 5.0E-01 1.48E-06 E,<
Toluene 5.2E-03 1.2E-01 6.6E-01 1.97E-06 E
X lenes 3.6E-03 8.5E-02 4.5E-01 1.35E-06 E
NO„control is via ignition timing retard.
Emission Factor Emission Factor
Greenhouse Gases Factor Quality Greenhouse Gases Factor Quality
Pollutant Ib! r t Ib/h -hr Ratin Pollutant Ib/hr Ib/ r t Ib/h hr Rating
Carbon Dioxide(CO2) 3.8E+05 1.9E+02 0.31 NA Carbon Dioxide(CO2) 2.8E+05 1.4E+02 0.23 NA
Methane(CH4) 2.1E+01 1.1E-02 0.0001 NA Methane(CH4) 1.3E+03 6.3E-01 0.004 NA
Nitrous Oxide(N20) 3.1 E+00 1.5E-03 0.00001 NA Nitrous Oxide(N20) 3.1 E+00 1.5E-03 0.00001 NA
LGD2008 Revision A dated June 30,2008
Pollutants in red are federally regulated hazardous air pollutants(HAPs)only. All other toxic/hazardous air pollutants are regulated as both HAPs and TAPs.
Factor quality ratings containing"<"indicate an AP-42 emission factor based on test results being below detection.
Emission factors for criteria and toxic/hazardous pollutants are from AP-42 Chapter 3.4,Large Stationary Diesel and All Stationary Dual-fuel Engines,dated October 1996.
Emission factors for greenhouse gases are from DAQ's Greenhouse Gas Emission Guidelines:Stationary Combustion Sources,June 2008,except for CH4, M
which uses AP-42,Chapter 3.4,Large Stationary Diesel and All Stationary Dual-fuel Engines,dated October 1996. WDENR
Carbon dioxide emission factor for dual-fuel engines is calculated based on 95%natural gas and 5%diesel,per AP-42 Section 3.4,p.3.4-5,revised 10/96.
Hourly emission rates for all pollutants are based on the hourly engine output.Annual emissions are based on the annual engine output.
Daily emissions are based on operation at the hourly output rate for 24 hours.

PERDUE FARMS,INC. - LEWISTON PROCESSING �
` Y 19
�yf'
Year- 2010
ACTUAL CALCULATIONS FOR TSP )Gf'
tfwu .00J 31, 3 7lti�yrea�^
PROCESS DESCRIPTION ES Chickens Control* TSP Emission TSP Actual TSP Actual
LEWISTON PROCESSING # Processed Efficiency Factor(lb/BIRD) Emissions Ib/yr LB/HR
RECEIVING LINE#1 ES 1 32,378,938 0.001 0.0003 9.71 0.0023
RECEIVING LINE#2 ES 2 32,378,938 0.001 0.0003 9.71 0.0023
RECEIVING LINE#3 IES 3 1 32,378,9381 0.001 0.00031 9.71 0.0023
TSP 29.14
Total in lbs/Yr
In Tons Year
0.015
*Efficiency Factors
a.Bagfilter contol(1-.999)_.001% ;J S a7
*Emission Factors
a.Engineering estimate of I00lb/hr per 100,000 chikens a day processed. Emission Factor based on this of.0003 lb/hr
per bird. tT►'1 i.�/f. �t•t LS ` N enl� OVC4 C
b.No%of TSP is known to be PM 10
cy

PERDUE FARMS,INC.-LEWISTON PROCESSING
ACTUAL/POTENTIAL CALCULATIONS FOR AMMONIA
PROCESS DESCRIPTION ES In Tons I Control* Ammonia Emission Ammonia Actual Ammonia Actual
LEWISTON PROCESSING # I Efficient Factor lb/ton EmissionsLB/YR EmissionsLB/HR
FUGITIVE EMISSIONS IES 6,7 1 11.081 1 2000 13758 1.570547945
Ammonia 13758
Total in Ibs/Yr
In Tons Year
6.879
*Efficiency Factors
13758 pounds of Andyrous Ammonia was received in 2010.
Actual equals Potential

PERDUE FARMS, INC. - LEWISTON PROTEIN CONVERSION
Protein Conversion Emissions Inventory
Year- 2010
ACTUAL CALCULATIONS FOR TSP
PROCESS DESCRIPTION In Tons Control* TSP Emission TSP Actual TSP ACT.
LEWISTON PROTEIN CONV. Efficiency Factor lb/ton Emissions LB/HR
POULTRY MEAL SILO ES16 8,004 0.001 0.27 2.16 0.0003
POULTRY MEAL SILO ES11 8,004 0.001 0.27 2.16 0.0003
POULTRY MEAL SILO ES15 8,004 0.001 0.27 2.16 0.0003
POULTRY MEAL SILO ES12 8,004 0.001 0.27 2.16 0.0003
POULTRY MEAL CONVEYANCE ES17 48,026 1 0.27 12967.02 1.8891 ftuy Liio�li h�G 1�!/S�f / ;Sf
POULTRY MEAL SILO ES14 8,004 0.001 0.27 2.16 0.0003 '
POULTRY MEAL SILO ES13 8,004 0.001 0.27 2.16 0.0003 a1sv P.v��
POU Y MEAL�RAD 48,0 6 �0.00 / 0 212.,W0,069 �POUL•TRY MEAL LOADOUT ES19 ,47,601 1< 0.27 pal4 1.6852 o'v'sth ro&
-c+
TSP 10
24560.0 Total in lbs/Yr
In Tons Year
*Efficiency Factors
a.Bagfilter contol(1-.999)_.001%
!VC, 'V Q/►1'115Sb5h
J fhcvr. S

Raw Tons Processed Jan-10 Feb-10 Mar-10 Apr-10 May-10 Jun-10 Jul-10 Aug-10 Sept-10 Oct-10 Nov-10 Dec-10 2010 Total
Offa 1 13,965 12,410 12,311 16,599 14,318 14,138 17,249 13,219 13,791 17,148 11,993 13,891 171,030
Feather 4,059 3,093 3,171 4,004 4,088 3,440 4,254 3,599 3,562 4,601 3,051 3,235 44,155
Total 18,024 15,502 15,482 20,603 18,406 17,577 21,503 16,818 17,353 21,749 15,043 17,126 215,186

Facility Total CY 2010 Emission Summary Facility Id : 0800081
Green House Gases Pollutants GHG
Actual Emissions TonsNear
Pollutant CAS 2010 2009 % Difference
Carbon Dioxide CO2 124389 40995.56 42990.38 -4.6401553%
Methane CH4 74-82-8 381.8205 382.0154 -0.051023014%
Nitrous Oxide N2O 10024972 0.0883 .1369 -35.500369%
CO2 equivalent(sum of individual GHG pollutant emission
times their 1995 IPCC Global Warming Potential(GWP), 44,490.14 metric tons
converted to metric tons
Criteria Pollutants
Actual Emissions onsNear
Pollutant CAS 2010 2009 % Difference
CO CO 30.3 28.26 7.2186804%
NOx NOx 42.81 53.69 -20.264477%
PM TSP TSP 16.57 21.67 -23.534842%
PM 10 PM 10 9.42 12.61 -25.29738%
PM2.5 PM2.5 0.98 5.02 -80.47809%
SO2 SO2 11.68 108.1 -89.19519%
VOC VOC 12.08 12.13 -0.41220272%
Hazardous Air Pollutants HAPS and/or Toxic Air Pollutants TAPs
Actual Emissions PoundsNear
Pollutant I CAS 1 2010 1 2009 % Difference
Antimony&Compounds total mass, inc elemental SB 0.0
Antimony Unlisted Compounds(Specify&Component of SBC SBC-Other T_ 0.0 3.4328 -100.0%
Arsenic& Compounds total mass of elemental AS,arsine and all inor anic compounds 0.0
Arsenic Unlisted Compounds(Specify&Component ASC-Other 0.0 .8631 -100.0%
of ASC
Beryllium&compounds(Total mass 0.0
Beryllium Compound, Unlisted BEC-Other 0.0 .01818 -100.0%
(Specify&Component of BEC
Cadmium&compounds total mass inc elemental metal 0.0
Cadmium Unlisted Compounds CDC-Other 0.0 .26024 -(Specify&Component of CDC 100.0%
Cobalt com ounds0.0
Cobalt Unlisted Compound (Specify&Component of COC) COC-Other 0.0 3.93628 -100.0%
Lead and Lead com ounds0.0
Lead Unlisted Compounds(Specify
and Component of PBC) pgC-Other 0.0 .98734 -99.99999%
Manganese&com ounds0.0
Manganese Unlisted Compounds MNC-Other __F_ 0.0 1.9616 -100.0%
(Specify&Component c MNC
Mercury&Compounds-all total mass, inc Hg Va or0.0
Mercury Unlisted Compounds HGC-Other 0.0 .07388 -100.0%
(Specify&Component of HGC
Nickel&Compounds, sum total mass, inc elementa10.0
Nickel Unlisted Compounds(Specify&Component of NIC NIC-Other 0.0 55.25168 -100.0%
Chromium VI Non-Specific Compounds, as Chrom I Com onent CRC 0.0
Chromium(VI) Non-Specific,
Unlisted (Specify&Component of NSCR6-Other 0.0 .55252 -100.0%
NSCR6&CRC) I I F
Chromium-AlI Total Inc Chromium I categories, metal and Others 0.0
Chromium (VI) Non-Specific,
Unlisted (Specify&Component of NSCR6-Other 0.0 .55252 -100.0%
NSCR6&CRC
Pol c clic Organic Matter(Specific Compounds from OAQPS for .61121
Benzo(a)pyrene(Component of 50-32-8 0.00121 .00139 -12.949638%

POMTV& POM7
Naphthalene (Component of POMTV 91-20-3 0.61 1.44886 -57.897934%
Pol c clic Organic Matter 7 PAH Com ounds for NIF .00121
Benzo(a)pyrene (Component of
POMTV& POM7) 50-32-8 0.00121 .00139 -12.949638%
Acetaldehyde 75-07-0 0.118 .136 -13.235298%
Acrolein 107-02-8 0.037 .043 -13.95349%
Ammonia as NH3 7664-41-7 13758.0 22169 -37.94037%
Benzene 71-43-2 4.98 5.53392 -10.009538%
Ethyl benzene 100-41-4 0.0 .04158 -100.0%
Fluorides(sum of all fluoride 16984-48-8 0.0 24,3892 -gg.ggggg%
compounds)
Formaldehyde 50-00-0 49.58 71.0893 -30.256731%
Hexane, n- 110-54-3 1183.0 1027.3 15.156229%
Methyl chloroform 71-55-6 0.0 .15432 -100.0%
Phosphorus Metal, Yellow or White 7723-14-0 0.0 6.18558 -100.0%
Polycyclic Organic Matter(Inc PAH,
dioxins
, etc. NC&AP 42 historic POM 1.0 1.92464 -48.042233%
amorphous lob
Selenium Compounds SEC 0.0 .4466 -100.0%
Toluene 108-88-3 1.32 5.57396 -76.31845%
X lene, o- 95-47-6 0.9 1.11128 -19.01231%
close

� � 1
Perdue Farms Incorporated
P.O.Box 460
Lewiston Woodville, NC 27849
www.perdue.com®
Office [phone]
June 24, 2011
Certified Mail: 7009 0820 0001 0821 1403
Return Receipt Requested
Mr. Robert Fisher, Regional Air Quality Supervisor
NCDENR
Division of Air Quality
Washington Regional Office
943 Washington Square Mall
Washington,North Carolina 27889
Subject: 2010 Emissions Inventory
Perdue Farms Incorporated
Cofield, Permit# 02875T29, Facility ID 4600082
Lewiston, Permit# 03085T28, Facility ID 800081
Dear Mr. Fisher:
Please find enclosed, emission inventory information for the above listed facilities that
were reported on-line. I have included the following forms for each facility: Aero
Confirmation& Inventory Summary, Certification Form, and spreadsheets for inventory
calculations (CY 2010).
I hope this meets with your approval and if you should have any questions regarding this
submittal please contact me at 252-348-4326. D n
Sincerely, U
JUN 2 8 2011
Wayne Black, Director Perdue DAQ WAR 0
Agribusiness Environmental
/enclosures: Air Emission Spreadsheets, Aero Confirmation& Inventory Summary,
Certification Form
i
2005 Perdue
A family Commitment to Quality Since igzo "

Inventory Certification Form(Title V)
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit• 03085
Lewiston,NC 27849 County.• Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
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 Wayne Black
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 STATEMENTe
m rt nt• Legally Responsible n Lmi aher all submissions are final.)
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 Si ed:
LrnintedName: Wayne Black
re:
This form applies to Title V facilities. IT'lis 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
EC EHE- 5
JUN 2 8 2011
Information on this Form cannot be held confidenti 1 =0W

Inventory Certification Form(Title V)
Facility Name: Perdue Farms Inc-Lewiston Facility ID : 0800081
3539 Governors Road Permit: 03085
Lewiston,NC 27849 County : Bertie
DAQ Region : WARD
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory-Calendar Year 2010
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 Wayne BlacF_ k
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).
afterCERTIFICATION STATEMENT:
(Iml2ortaUte Legally Responsible Official,read and sign
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 Si ed: -a,
Printed Name: Wayne Black
ISignature:
This form applies to Title V facilities. If trus facility is not classified as Title V,please telephone your regional office Emission
Inventory contact at once for proper forms R
E C E � W E
JUN 2 8 2011
Email address of Responsible Official: [e-mail]
DAQ WARO
Information on this Form cannot be held confidential
1

Higginbotham, Sheila
From: [e-mail]
Sent: Thursday, June 23, 2011 12:14 PM
Subject: Inventory submission confirmation --0800081
Dear Wayne Black
Your submittal of the 2010 emission inventory for Perdue Farms Inc - Lewiston, 0800081,
has been received by the North Carolina Division of Air Quality (DAQ).
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, 943 Washington Square Mall, Washington, NC 27889 by the
required due date in order for this submittal to be considered complete. If you have any
questions, please feel free to contact Mike Smithwick, in the Washington Regional Office,
at(252) 946-6481.
The Division of Air Quality thanks you for using AFRO, the on line emissions inventory
program.
Sincerely
DAQ
1

2010 EMISSIONS INVENTORY
PERDUE FARMS INCORPORATED
Lewiston, NORTH CAROLINA
Prepared for:
North Carolina Department of
Environment And Natural Resources

As entered in AERO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit : 03085
Lewiston,NC 27849 County : Bertie
DAQ Region : WARO
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
ES-1 One live poultry receiving and CS-1 bagfilter(2,100 square feet of filter area) CD-1
handling system
condenser(2488, square feet of surface
area) , condenser(2092 square feet of
One poultry by—product cooker surface area) ,condenser(1319 square
ES-10A.1 and one dual—use feather/poultry CS-11 feet of surface area) , condenser(1183 CD—lOD
by—product cooker square feet of surface area) ,2—stage
crossflow wet scrubber(500 gals/min
nom. liq. inject. rate/stage)filter mist
eliminator
ES-10A.2 One feather dryer and one
hydrolyzer
condenser(2488, square feet of surface
area) , condenser(2092 square feet of
surface area) , condenser(1319 square
ES—lOB Poultry by—product presses and CS-11 feet of surface area) , condenser(1183 CD-101)
preheater square feet of surface area) ,2—stage
crossflow wet scrubber(500 gals/min
nom. liq. inject. rate/stage)filter mist
eliminator
2—stage crossflow wet scrubber(500
ES-101) Process room air collection CS-5 gals/min nom. liq. inject. rate/stage)filter CD—lOD
mist eliminator
ES-10E Two liquid/fat evaporators
ES-11 One poultry meal storage silo CS-8 2 collapsible bagfilters(38 square feet of CD-11A, CD-11B
filter area each)
ES-12 One poultry meal storage silo CS-9 2 collapsible bagfilters(38 square feet of CD-12A,CD-12B
filter area each)
ES-13 One poultry meal storage silo CS-10 2 collapsible bagfilters (38 square feet of CD—13A, CD—13B
filter area each)
ES-14 One poultry meal storage silo CS-12 2 collapsible bagfilters (38 square feet of CD-14A, CD-14B
filter area each)
ES-15 One poultry meal storage silo CS-13 2 collapsible bagfilters(38 square feet of CD-15A, CD-15B
filter area each)
ES-16 One poultry meal storage silo CS-14 2 collapsible bagfilters(38 square feet of CD-16A, CD-16B
filter area each)
ES-19 Poultry meal loadout area(54
tons per hour capacity)
1

ES-2 One live poultry receiving and CS-2 bagfilter(2,100 square feet of filter area) CD-2
handling system
ES-22A One diesel—fired generator(2628
horsepower engine output)
ES-22B One diesel—fired generator(2628
horsepower engine output)
One natural gas—fired temporary,
back—up boiler(less than 90
ES-23 million Btu per hour maximum
heat input capacity) [NSPS,
Subpart Dc]
One natural gas—fired temporary,
back—up boiler(less than 90
ES-24 million Btu per hour maximum
heat input capacity) [NSPS,
Subpart Dc]
ES-3 One live poultry receiving and CS-3 bagfilter(2,100 square feet of filter area) CD-3
handling system
One No. 6 fuel—oil/natural
ES-4 gas—fired boiler(20.3 million Btu
per hour maximum heat input
capacity)
One No. 6 fuel—oil/natural
ES-5 gas—fired boiler(20.3 million Btu
per hour maximum heat input
capacity)
One packed bed scrubber(288 to 575
gallon per minute normal operating range)
One natural gas/saleable animal utilizing water,air, and filter media to
ES-8 fat/No.6 oil—fired boiler(84 CS-17 reduce PM and S02 emissions in the CD-10F
million Btu per hour maximum boilers and also used conditionally for
heat input capacity) additional control of noncondensibles
depending on fuel fired in the boilers for
the poultry processing equipment,
One packed bed scrubber(288 to 575
gallon per minute normal operating range)
One natural gas/saleable animal utilizing water,air, and filter media to
ES-9 fat/No.6 oil—fired boiler(84 CS-17 reduce PM and S02 emissions in the CD-1 OF
million Btu per hour maximum boilers and also used conditionally for
heat input capacity) additional control of noncondensibles
depending on fuel fired in the boilers for
the poultry processing equipment,
I—ES-6 Refrigeration system
I—ES-7 Propane—fired Singers for
singeing poultry
I—WWTP Wastewater Treatment System
IES17 IPoultry meal conveyance system
2

As entered in AERO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit: 03085
Lewiston,NC 27849 County : Bertie
DAQ Region : WARO
Emission Source & Operating Scenario List— See Instructions
*ES Group ID *ES ID *OS ID *OS Description
G-31 ES—IOB,ES-10A.1 30 cookers IOA and IOB
ES-1 19 live poultry receiving and handling
system
ES-10A.2 NONE NONE
ES-10D 31 _process room air collection
ES-10E NONE NONE
ES-11 11 poultry meal storage silo
ES-12 15 _poultry meal storage silo
ES-13 29 poultry meal storage silo
ES-14 17 poultry meal storage silo
ES-15 18 poultry meal storage silo
ES-16 32 poultry meal storage silo
ES-19 34 poultry meal loadout area(54 tons per
hour capacity)
ES-2 20 live poultry receiving and handling
system
ES-22A 35 Generator for Emergency Power/
Peak Shaving
ES-22B 36 Generator for Emergency Power/
Peak Shaving
One natural gas—fired temporary,
ES-23 40 back—up boiler(less than 90 million
Btu per hour maximum heat input
capacity) [NSPS,Subpart Dc]
One natural gas—fired temporary,
ES-24 41 back—up boiler(less than 90 million
Btu per hour maximum heat
ES-3 21 live poultry receiving and handling
system
4 No. 6 fuel—oil fired boilers(20.3
million Btu per hour heat input)
ES-4 One No. 6 fuel—oil/natural gas—fired
38 boiler(20.3 million Btu per hour
maximum heat input
ES-5 5 No. 6 fuel—oil fired boilers(20.3
million Btu per hour heat input)
39
3

One No. 6 fuel—oil/natural gas—fired
boiler(20.3 million Btu per hour
maximum heat input
natural gas/saleable animal fat/no.6 oil
22 fired boiler(84 million Btu per hour
ES-8 heat input)
natural gas/saleable animal fat/no.6 oil
23 fired boiler(84 million Btu per hour
heat input)
natural gas/saleable animal fat/no.6 oil
24 fired boiler(84 million Btu per hour
ES-9 heat input)
natural gas/saleable animal fat/no.6 oil
25 fired boiler(84 million Btu per hour
heat input)
I—ES-6 26 refrigeration system
I—ES-7 27 propane—fired Singers for singeing
poultry
I—WWTP 37 Wastewater Treatment System
MS17 33 1poultry meal conveyance system
4

As entered in AERO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit : 03085
Lewiston,NC 27849 County : Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
1. Emission Source ID(from permit)or Group G-31 consisting of ES-10B, ES-10A.1
Emission Source Group ID
2. Emission Source Description: cookers IOA and IOB
3. Operating Scenario ID/Description: OS—30/cookers 10A and 1013
4. SCC Number/Description: 30203803/Animal/Poultry Rendering
5. Throughput/units in 2010: 215186 TON/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-11 CD-10D One two—stage crossflow wet scrubber(500 gallons per minute nominal
liquid injection rate per stage)and a dry filter mist eliminator
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-10 IVERTICAL STACK 62.5 1.18 1 93 43.3 2841.14 stack
5

Operating Scenario: OS—30 Emission Source/Group ID: G-31
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
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.
010 O10 010 010 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
2010
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)
2010
CO CO 08 0
NOx NOx 08 0
TSP TSP 08 0
PM10 PM10 08 0
PM2.5 PM2.5 08 0
S02 S02 08 0
VOC VOC 9.87 08 85 0.0917 AFTER
HAP/TAPCAS Emissions Emission Estimation Control Emission
Pollutants (In HAP/TAPS Efficiency EF Control
(see instructions) Method Code
Alphabetical Order) (Pounds/Year) (Net after all controls) Factor
See Instructions
2010
6

As entered in AERO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit : 03085
Lewiston,NC 27849 County : Bertie
DAQ Region : WARO
J
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
1. Emission Source ID(from permit)or ES-1
Emission Source Group ID
2. Emission Source Description: One live poultry receiving and handling system
3. Operating Scenario ID/Description: OS— 19/live poultry receiving and handling system
4. SCC Number/Description: 30203805/Animal/Poultry Rendering
5. Throughput/units in 2010: 32378938 EACH/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-1 CD-1 One ba filter(2,800 square feet of filter area
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-1 VERTICAL STACK 14.4 2.25 60 5.71 1362.2 stack
7

Operating Scenario: OS— 19 Emission Source/Group ID: ES-1
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
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% ept.—Nov. 25%
010 010 �010 �010
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
2010
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)
2010
CO CO 08 0
NOx NOx 08 0
TSP TSP 0 03 99.9 0.0003 BEFORE
PM10 PM10 0 03 99.9 0.0003 BEFORE
PM2.5 PM2.5 08 0
S02 S02 08 0
VOC VOC 08 0
HAP/TAP Emissions Emission Control
Estimation Efficiency Emission EF Control
Pollutants (In (see instructions)CAS HAP/TAPS Method Code Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2010
8

As entered in AFRO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit : 03085
Lewiston,NC 27849 County : Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
1. Emission Source ID(from permit)or ES-10D
Emission Source Group ID
2. Emission Source Description: Process room air collection
3. Operating Scenario ID/Description: OS—31/process room air collection
4. SCC Number/Description: 30299998/*Other Not Specified
5. Throughput/units in 2010: 215186 TON/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /° Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-5 CD-10D One two—stage crossflow wet scrubber(500 gallons per minute nominal
liquid injection rate per stage)and a dry filter mist eliminator
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-10 VERTICAL STACK 62.5 1.18 93 43.3 2841.14 stack
9

Operating Scenario: OS—31 Emission Source/Grow ID:ES—IOD
P g P
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 250�o 25"�u une—Aug. 25"�o �010
ept.—Nov.
O10 �arch—May
10 010 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
2010
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)
2010
CO CO 08 0
NOx NOx 08 0
TSP TSP 08 0
PM10 PM10 08 0
PM2.5 PM2.5 08 0
SO2 SO2 08 0
VOC VOC 0.1 08 85
HAP/TAP Emissions Emission Control
CAS Estimation Emission EF Control
Pollutants (In HAP/TAPS Efficiency
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2010
10

As entered in AFRO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit : 03085
Lewiston,NC 27849 County : Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
1. Emission Source ID(from permit)or ES—II
Emission Source Group ID
2. Emission Source Description: One poultry meal storage silo
3. Operating Scenario ID/Description: OS— 11/poultry meal storage silo
4. SCC Number/Description: 30299998/*Other Not Specified
5. Throughput/units in 2010: 8004 TON/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 100
Device or Stack):
8. Control Device information
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-8 CD-11A One collapsible ba filter 38 square feet of filter area
2 CS-8 CD-1113 One collapsible ba filter 38 square feet of filter area
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-11 IVERTICAL STACK 53 1.18 120 7A 465.86 stack
11

Operating Scenario: OS— 11 Emission Source/Group ID:ES—11
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
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% �010
ept.—Nov. 25%
010 010 �010
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
2010
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)
2010
CO CO 08 0
NOx NOx 08 0
TSP TSP 0 08 99.9 027 BEFORE
PM10 PM10 0 08 99.9 0.27 BEFORE
PM2.5 PM2.5 08 0
S02 S02 08 0
VOC VOC 08 0
HAP/TAP CAS Emissions Emission Estimation Control
ffi Emission
Pollutants (In HAP/TAPS Efficiency EF Control
(see instructions) Method Code
Alphabetical Order) (Pounds/Year) (Net after all controls) Factor
See Instructions
2010
12

As entered in AERO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit: 03085
Lewiston,NC 27849 County : Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
1. Emission Source ID(from permit)or ES-12
Emission Source Group ID
2. Emission Source Description: One poultry meal storage silo
3. Operating Scenario ID/Description: OS— 15/poultry meal storage silo
4. SCC Number/Description: 30299998/*Other Not Specified
5. Throughput/units in 2010: 8004 TON/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-9 CD-12A One collapsible ba filter 38 square feet of filter area
2 CS-9 CD-12B One collapsible ba filter 38 square feet of filter area
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-12 IVERTICAL STACKI 51 1 0.94 120 12.1 503.82 stack
13

Operating Scenario: OS— 15 Emission Source/Group ID: ES-12
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
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% ept.—Nov. 25%
2010 010 �010 �010
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
2010
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)
2010
CO CO 08 0
NOx NOx 08 0
TSP TSP 0 08 99.9 0.27 BEFORE
PM10 PM10 0 08 99.9 0.27 BEFORE
PM2.5 PM2.5 08 0
S02 S02 08 0
VOC VOC 08 0
HAP/TAP Emissions Emission Control
Pollutants (in CAS HAP/TAPS Estimation Emission
(see instructions) Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2010
14

As entered in AFRO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit: 03085
Lewiston,NC 27849 County :Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
1. Emission Source ID(from permit)or ES-13
Emission Source Group ID
2. Emission Source Description: One poultry meal storage silo
3. Operating Scenario ID/Description: OS—29/poultry meal storage silo
4. SCC Number/Description: 30203805/Animal/Poultry Rendering
5. Throughput/units in 2010: 8004 TON/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-10 CD-13A One collapsible ba filter 38 square feet of filter area
2 CS-10 CD-13B One collapsible ba filter 38 square feet of filter area
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feettsec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-13 IVERTICAL STACKI 53 1 1.18 120 7.1 465.86 stack
15

Operating Scenario: OS—29 Emission Source/Group ID:ES-13
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
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% M 25% une—Aug. 25% ept.—Nov. 25%
010 �arch— ay
10 �010 �010
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
2010
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)
2010
CO CO 08 0
NOx NOx 08 0
TSP TSP 0 08 99.9 0.27 BEFORE
PM10 PM10 0 08 99.9 0.27 BEFORE
PM2.5 PM2.5 08 0
S02 S02 08 0
VOC VOC 08 0
HAP/TAP Emissions Emission Control
Pollutants (in CAS HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2010
16

As entered in AFRO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit : 03085
Lewiston,NC 27849 County : Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
1. Emission Source ID(from permit)or ES-14
Emission Source Group ID
2. Emission Source Description: One poultry meal storage silo
3. Operating Scenario ID/Description: OS— 17/poultry meal storage silo
4. SCC Number/Description: 30299998/*Other Not Specified
5. Throughput/units in 2010: 8004 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
(%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-14A One collapsible ba filter 38 square feet of filter area
2 CS-12 CD-14B One collapsible ba filter 38 square feet of filter area
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-14 IVERTICAL STACK 51 0.94 120 12.1 503.82 1 stack
17

Operating Scenario: OS — 17 Emission Source/Group ID: ES-14
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
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 25o�a 25% une—Aug. 25% ept.—Nov. 25%
010 �arch—May
10 �010 �010
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/Yea See Instructions all controls
2010
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)
2010
CO CO 08 0
NOx NOx 08 0
TSP TSP 0 08 99.9 0.27 BEFORE
PM10 PM10 0 08 99.9 0.27 BEFORE
PM2.5 PM2.5 08 0
S02 S02 08 0
VOC VOC 08 0
Emission
HAP/TAPCAS Emissions Estimation Control Emission
Pollutants (In HAP/TAPS Efficiency EF Control
(see instructions) Method Code
Alphabetical Order) (Pounds/Year) (Net after all controls) Factor
See Instructions
2010
18

As entered in AFRO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit: 03085
Lewiston,NC 27849 County :Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
1. Emission Source ID(from permit)or ES-15
Emission Source Group ID
2. Emission Source Description: One poultry meal storage silo
3. Operating Scenario ID/Description: OS— 18/poultry meal storage silo
4. SCC Number/Description: 30299998/*Other Not Specified
5. Throughput/units in 2010: 8004 TON/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 100
Device or Stack):
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-13 CD-15A One collapsible ba filter 38 square feet of filter area
2 CS-13 CD-15B One collapsible ba filter 38 square feet of filter area
9.Emission Release Point RP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-15 IVERTICAL STACK 53 1 1.18 120 7.1 465.86 stack
19

Operating Scenario: OS— 18 Emission Source/Group ID:ES-15
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
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 Throuh ut:
an—Feb +Dec Y arch—Ma une—Aug. o �010
ept.—Nov. o
�010 25% 010 25% �010 25/0 2i /�
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/Ye See Instructions all controls
2010
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficient Emission
(NAAQS) y Ef Control
Pollutants Code Pollutants Method Code (Net after Factor
(Tons/Year) (See Instructions) all controls)
2010
CO CO 08 0
NOx NOx 08 0
TSP TSP 0 08 99.9 0.27 BEFORE
PM10 PM10 0 08 99.9 0.27 BEFORE
PM2.5 PM2.5 08 0
S02 S02 08 0
VOC VOC 08 0
HAP/TAP CAS Emissions Emission Estimation Control Emission
Pollutants (In HAP/TAPS Efficiency EF Control
(see instructions) Method Code
Alphabetical Order) (Pounds/Year) (Net after all controls) Factor
See Instructions
2010
20

As entered in AFRO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit : 03085
Lewiston,NC 27849 County :Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
1. Emission Source ID(from permit)or ES-16
Emission Source Group ID
2. Emission Source Description: One poultry meal storage silo
3. Operating Scenario ID/Description:tion: OS—32/ oul meal storage silo
P g P P �3' g
4. SCC Number/Description: 30203805/Animal/Poultry Rendering
5. Throughput/units in 2010: 8004 TON/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information
Order CS—ID CD ID Control Device Description
as listed inpermit)
I CS-14 CD-16A One collapsible ba filter 38 square feet of filter area
2 CS-14 CD-16B One collapsible ba filter 38 square feet of filter area
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-16 VERTICAL STACK 5> 1.18 120 7.1 465.86 stack
21

Operating Scenario: OS—32 Emission Source/Group 1D: ES-16
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
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% ept.—Nov. 25'Yo
010 010 �010 �010
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
Gtl(: C 1S GHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Ye See Instructions all controls
2010
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)
2010
CO CO 08 0
NOx NOx 08 0
TSP TSP 0 08 99.9 0.27 BEFORE
PM10 PM10 0 08 99.9 0.27 BEFORE
PM2.5 PM2.5 08 0
S02 S02 08 0
VOC VOC 08 0
HAP/TAP Emissions Emission Control
CAS Estimation Emission
Pollutants (In HAP/TAPS Efficiency EF Control
(see instructions) Method Code
Alphabetical Order) (Pounds/Year) (Net after all controls) Factor
See Instructions
2010
22

As entered in AFRO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit : 03085
Lewiston,NC 27849 County :Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
1. Emission Source ID(from permit) or ES-19
Emission Source Group ID
2. Emission Source Description: Poultry meal loadout area(54 tons per hour capacity)
3. Operating Scenario ID/Description: OS—34/poultry meal loadout area(54 tons per hour capacity)
4. SCC Number/Description: 30203805/Animal/Poultry Rendering
5. Throughput/units in 2010: 47601 TON/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sul fiir %Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter ft (F) (Feet/see) (Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-19 FUGITIVE(NO 1 60 Area= 1 three sided enclosure
STACK
23

Operating Scenario: OS—34 Emission Source/Group ID:ES-19
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
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 Throuh ut:
an—Feb +Dec y arch—Ma une—Aug. ° �010
ept.—Nov.
�010 25% O10 25% 2010 25/o 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/Ye See Instructions all controls
2010
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)
2010
CO CO 08
NOx NOx 08
TSP TSP 6.43 08 0.27
PM10 PM10 6.43 08 0.27
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP Emissions Emission Control
CAS [ Estimation Emission
Pollutants (In HAP/TAPS Efficiency EF Control
Alphabetical Order) (Pounds/Year) (Net after all controls)
(see instructions) Method Code Factor
See Instructions
2010
24

As entered in AERO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit : 03085
Lewiston,NC 27849 County : Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
1. Emission Source ID(from permit)or ES-2
Emission Source Group ID
2. Emission Source Description: One live poultry receiving and handling system
3. Operating Scenario ID/Description: OS—20/live poultry receiving and handling system
4. SCC Number/Description: 30203805/Animal/Poultry Rendering
5. Throughput/units in 2010: 32378938 EACH/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information :
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-2 CD-2 One ba filter(2,800 square feet of filter area
9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-2 IVERTICAL STACKI 14.4 2.25 60 1 4.51 1076 stack
25

Operating Scenario: OS—20 Emission Source/Group ID: ES-2
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
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.—nog. 25%
010 �arch—May
10 �010 2010
13. Actual Emissions ner 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
2010
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)
2010
CO CO 08 0
NOx NOx 08 0
TSP TSP 0 08 99.9 0.0003 BEFORE
PM10 PM10 0 08 99.9 0.0003 BEFORE
PM2.5 PM2.5 08 0
S02 S02 08 0
VOC VOC 08 0
HAP/TAP CAS Emissions Estimation timation Control Emission
Pollutants (In HAP/TAPS Efficiency EF Control
(see instructions) Method Code
Alphabetical Order) (Pounds/Year) (Net after all controls) Factor
See Instructions
2010
26

As entered in HERO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit: 03085
Lewiston,NC 27849 County : Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
1. Emission Source ID(from permit)or ES-22A
Emission Source Group ID
2. Emission Source Description: One deisel—fired generator(2628 horsepower engine output)
3. Operating Scenario ID/Description: OS—35/Generator for Emergency Power/Peak Shaving
4. SCC Number/Description: 20200401/Diesel
5. Throughput/units in 2010: 128 HR/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 inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
EP22A FUGITIVE(NO 1 72 TArea— 1 Fugitive Emissions
STACK from Genarator
27

Operating Scenario: OS—35 Emission Source/Group ID: ES-22A
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
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.—Nor. 25%
010 1 010 �010 2010
13. Actual Emissions per Pollutant Listed :
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG GHG Estimation Efficiency Emission
Pollutants CAS y Ef Control
Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2010
Carbon Dioxide CO2 124389 190 08
Methane CH4 74-82-8 0.011 08
Nitrous Oxide N20 10024972 0.0016 08
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)
2010
CO CO 0.93 08
NOx NOx 4 08
TSP TSP 0.12 08
PM10 PM10 0.12 08
PM2.5 PM2.5 0.12 08
S02 S02 0.07 08
VOC VOC 0.11 08
CAS Emissions Emission Control
HAP/TAP (see HAP/TAPS Estimation Efficiency Emission EF Control
Pollutants (In Alphabetical Order) instructions) (Pounds/Year) Method Code (Net after all Factor
See Instructions) controls)
2010
Acetaldehyde 75-07-0 0.059 09
Acrolein 107-02-8 0.019 09
Benzene 71-43-2 1.8 09
Benzo(a)pyrene(Component of 50-32-8 0.00061 09
POMTV POM7
Formaldehyde 50-00-0 0.19 09
Naphthalene(Component of 91-20-3 0.31 09
POMT
Polycyclic Organic Matter(Inc
PAH,dioxins,etc.NC AP 42 POM 0.5 09
historic amorphous lob
28

As entered in AERO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit: 03085
Lewiston,NC 27849 County :Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
1. Emission Source ID(from permit)or ES-22B
Emission Source Group ID
2. Emission Source Description: One deisel—fired generator(2628 horsepower engine output)
3. Operating Scenario ID/Description: OS—36/Generator for Emergency Power/Peak Shaving
4. SCC Number/Description: 20200401/Diesel
5. Throughput/units in 2010: 127 I-IR/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /, Sulfur °/,Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
FUGITIVE(NO Generator Engine
EP22B STACK 1 72 Area= 1 Emissions
30

Toluene 108-88-3 0.66 09
Xylene, o— 95-47-6 0.45 09
29

Operating Scenario: OS —36 Emission Source/Group ID: ES-22B
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
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% ept.—Nov. 25%
2010 010 �010 �010
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
2010
Carbon Dioxide CO2 124389 190 08
Methane CH4 74-82-8 0.011 08
Nitrous Oxide N20 10024972 0.0015 08
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)
2010
CO CO 0.92 08
NOx NOx 4 08
TSP TSP 0.12 08
PM10 PM10 0.12 08
PM2.5 PM2.5 0.12 08
S02 S02 0.07 08
VOC VOC 0.11 08
CAS Emissions Emission Control
HAP/TAP Estimation Efficiency Emission
Pollutants (In Alphabetical Order) instructions) (Pounds/Year)(see HAP/TAPS Method Code (Net after all Factor EF Control
See Instructions controls)
2010
Acetaldehyde 75-07-0 0.059 09
Acrolein 107-02-8 0.018 09
Benzene 71-43-2 1.8 09
Benzo(a)pyrene(Component of 50-32-8 0.0006 09
POMTV POM7
Formaldehyde 50-00-0 0.18 09
Naphthalene(Component of 91-20-3 0.3 09
POMT
Polycyclic Organic Matter(Inc
PAH, dioxins,etc.NC AP 42 POM 0.5 09
historic amorphous lob
31

Toluene 108-88-3 0.66 09
X lene,o— 95-47-6 0.45 09
32

As entered in AERO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit: 03085
Lewiston,NC 27849 County : Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
1. Emission Source ID(from permit) or ES-23
Emission Source Group ID
2. Emission Source Description: One natural gas—fired temporary,back—up boiler(less than 90 million Btu per
hour maximum heat input capacity) [NSPS, Subpart Dc]
3. Operating Scenario ID/Description: OS—40/One natural gas—fired temporary,back—up boiler(less than 90 million
Btu per hour maximum heat input capacity) [NSPS,Subpart Dc]
4. SCC Number/Description: 10200602/Natural Gas
5. Throughput/units in 2010: 58.3 E6FT3/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content 1020 Btu/CF
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
FTET7,VERTICAL STACK 15 2.4 490 6.5 1764.31 stack
33

Operating Scenario: OS —40 Emission Source/Group ID: ES-23
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
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% 250�o une—Aug. 25% ept.—Nov. 25%
010 farch—May
10 �010 �010
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
2010
Carbon Dioxide 124389 3502.72 09
CO2
Methane CH4 74-82-8 0.0661 09
Nitrous Oxide N20 10024972 0.0066 09
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)
2010
CO CO 2.45 09
NOx NOx 1.46 09
TSP TSP 0.22 09
PM10 PM10 0.17 09
PM2.5 PM2.5 0.06 09
S02 S02 0.02 09
VOC VOC 0.16 09
HAP/TAP Emissions Emission Control
Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission
EF Control
Alphabetical Order) (Pounds/Year)
(see instructions) Method Code (Net after all Factor
See Instructions controls)
2010
Benzene 71-43-2 0.122 09
Formaldehyde 50-00-0 4.37 09
Hexane, n— 110-54-3 105 09
34

As entered in AERO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit : 03085
Lewiston,NC 27849 County :Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
1. Emission Source ID(from permit)or ES-24
Emission Source Group ID
2. Emission Source Description: One natural gas—fired temporary,back—up boiler(less than 90 million Btu per
hour maximum heat input capacity) [NSPS, Subpart Dc]
3. Operating Scenario ID/Description: OS—41/One natural gas—fired temporary,back—up boiler(less than 90 million
Btu per hour maximum heat
4. SCC Number/Description: 10200602/Natural Gas
5. Throughput/units in 2010:
(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 RP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
ES24 VERTICAL STACK 15 2.4 490 17.16 4658.9 stack
35

Operating Scenario: OS—41 Emission Source/Group ID: ES-24
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
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%
010 010 2010 O10
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
2010
Criteria Emissions— Emission Control
Aene Pollutant Criteria Estimation Efficiency Emission
. Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2010
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP Emissions Emission Control
CAS Estimation Emission
Pollutants (In HAP/TAPS Efficiency EF Control
(see instructions) Method Code
Alphabetical Order) (Pounds/Year) (Net after all controls) Factor
See Instructions
2010
36

As entered in AERO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit : 03085
Lewiston,NC 27849 County : Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
1. Emission Source ID(from permit)or ES-3
Emission Source Group ID
2. Emission Source Description: One live poultry receiving and handling system
3. Operating Scenario ID/Description: OS—21/live poultry receiving and handling system
4. SCC Number/Description: 30203805/Animal/Poultry Rendering
5. Throughput/units in 2010: 32378938 EACH/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 100
Device or Stack):
8. Control Device Information :
Order CS—ID CD ID Control Device Description
as listed inpermit)
1 CS-3 CD-3 One ba filter 2,800 square feet of filter area
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry tines):
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-3 IVERTICAL STACKI 14.4 2.25 1 60 4.51 1076 1 stack
37

Operating Scenario: OS—21 Emission Source/Group ID:ES-3
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
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%
010 1 O10 �010 2010
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/Ye az See Instructions) all controls)
2010
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAAQS) Ef Control
Pollutants Code Pollutants Method Code (Net after Factor
(Tons/Year) (See Instructions) all controls)
2010
CO CO 08 0
NOx NOx 08 0
TSP TSP 0 08 99.9 0.0003 BEFORE
PM10 PM10 0 08 99.9 0.0003 BEFORE
PM2.5 PM2.5 08 0
S02 S02 08 0
VOC VOC 08 0
HAP/TAP Emissions Emission Control
CAS Estimation Emission
Pollutants (In HAP/TAPS Efficiency EF Control
(see instructions) Method Code
Alphabetical Order) (Pounds/Yeaz) (Net after all controls) Factor
See Instructions
2010
38

As entered in HERO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit: 03085
Lewiston,NC 27849 County : Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
1. Emission Source ID(from permit)or ES-4
Emission Source Group ID
2. Emission Source Description: One No. 6 fuel—oil/natural gas—fired boiler(20.3 million Btu per hour
maximum heat input capacity)
3. Operating Scenario ID/Description: OS—4/No. 6 fuel—oil fired boilers(20.3 million Btu per hour heat input)
4. SCC Number/Description: 1020040 1/Residual Oil(No. 6)
5. Throughput/units in 2010:
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-4 IVERTICAL STACKI 20 1 2 400 19.1 3600.26 stack
39

Operating Scenario: OS—4 Emission Source/Group ID: ES-4
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 250�o 25"�o une—Aug. 25"�u �010
ept.—Noy. 25,�o
O10 �arch—May
10 010
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
2010
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)
2010
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP CAS Emissions Emission Estimation Control Emission
Pollutants (In HAP/TAPS Efficiency EF Control
d d C
(see instructions) Method Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2010
40

As entered in AERO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit: 03085
Lewiston,NC 27849 County : Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
1. Emission Source ID(from permit)or ES-4
Emission Source Group ID
2. Emission Source Description: One No. 6 fuel—oil/natural gas—fired boiler(20.3 million Btu per hour
maximum heat input capacity)
3. Operating Scenario ID/Description: OS—38/One No. 6 fuel—oil/natural gas—fired boiler(20.3 million Btu per hour
maximum heat input
4. SCC Number/Description: 10200602/Natural Gas
5. Throughput/units in 2010: 65.59 E6FT3/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content 1020 Btu/CF
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 inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-4 VERTICAL STACK 20 1 2 400 19.1 3600.26 stack
41

Operating Scenario: OS—38 Emission Source/Group ID:ES-4
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
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.
010 O10 010 2010 25%
13. Actual Emissions ger 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
2010
Carbon Dioxide 124389 3940.71 09
CO2
Methane CH4 74-82-8 0.0743 09
Nitrous Oxide 20 10024972 0.0074 09
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)
2010
CO CO 2.75 09
NOx NOx 3.28 09
TSP TSP 0.25 09
PM10 PM10 0.19 09
PM2.5 PM2.5 0.06 09
S02 S02 0.02 08
VOC VOC 0.18 09
HAP/TAP Emissions Emission Control
CAS Estimation Efficiency Emission
Pollutants (in HAP/TAPS EF Control
Alphabetical Order)
(see instructions) (Pounds/Year) Method Code (Net after all Factor
See Instructions controls)
2010
Benzene 71-43-2 0.138 09
Formaldehyde 50-00-0 4.92 09
Hexane n— 110-54-3 118 09
42

As entered in AERO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit : 03085
Lewiston,NC 27849 County : Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
1. Emission Source ID(from permit)or ES-5
Emission Source Group ID
2. Emission Source Description: One No. 6 fuel—oil/natural gas—fired boiler(20.3 million Btu per hour
maximum heat input capacity)
3. Operating Scenario ID/Description: OS—5/No. 6 fuel—oil fired boilers(20.3 million Btu per hour heat input)
4. SCC Number/Description: 1020040 1/Residual Oil(No. 6)
5. Throughput/units in 2010:
(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 MERP 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(Acim)
Rectangle(L x W)
in 0.1 feet)
EP-5 VERTICAL STACK 20 2 400 19.1 3600.26 stack
43

Operating Scenario: OS—5 Emission Source/Group ID:ES-5
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
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 une—Aug. �010
ept.—Nov. o
010 25�° O10 25% �010 2��° 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
2010
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficient Emission
(NAAant Code Pollutants Method Code y Ef Control
Pollutants (Net after Factor
(Tons/Year) (See Instructions) all controls)
2010
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 Estimation on Control Emission
Pollutants (In HAP/TAPS Efficiency EF Control
(see instructions) Method Code
Alphabetical Order) (Pounds/Year) (Net after all controls) Factor
See Instructions
2010
44

As entered in AERO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit: 03085
Lewiston,NC 27849 County : Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
1. Emission Source ID(from permit)or ES-5
Emission Source Group ID
2. Emission Source Description: One No. 6 fuel—oil/natural gas—fired boiler(20.3 million Btu per hour
maximum heat input capacity)
3. Operating Scenario ID/Description: OS—39/One No. 6 fuel—oil/natural gas—fired boiler(20.3 million Btu per hour
maximum heat input
4. SCC Number/Description: 10200602/Natural Gas
5. Throughput/units in 2010: 65.59 E6FT3/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur ro
Ash Heat Content 1020 Btu/CF
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-5 VERTICAL STACK 20 2 400 19.1 3600.26 stack
45

Operating Scenario: OS—39 Emission Source/Group ID: ES-5
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
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%arch—May 25% ept.—Nov. 25%
O10 �010 010 �010
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
2010
Carbon Dioxide 124389 3940.71 09
(CO2
Methane CH4 74-82-8 0.0743 09
Nitrous Oxide N20 10024972 0.0074 09
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)
2010
CO CO 2.75 09
NOx NOx 3.28 09
TSP TSP 0.25 09
PM10 PM10 0.19 09
PM2.5 PM2.5 0.06 09
S02 S02 0.02 08
VOC VOC 0.16 09
HAP/TAP Emissions Emission Control
Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission EF Control
Alphabetical Order)
(see instructions) (Pounds/Year) Method Code (Net after all Factor See Instructions controls)
2010
Benzene 71-43-2 0.138 09
Formaldehyde 50-00-0 4.92 09
Hexane, n— 110-54-3 118 09
46

As entered in HERO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit: 03085
Lewiston,NC 27849 County : Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
1. Emission Source ID(from permit) or ES-8
Emission Source Group ID
2. Emission Source Description: One natural gas/saleable animal fat/No.6 oil—fired boiler(84 million Btu per
hour maximum heat input capacity)
3. Operating Scenario ID/Description: OS—22/natural gas/saleable animal fat/no.6 oil fired boiler(84 million Btu per
hour heat input)
4. SCC Number/Description: 10200602/Natural Gas
5. Throughput/units in 2010: 233.86 E6FT3/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) ro
Sulfur /o Ash Heat Content 1020 Btu/CF
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-8 VERTICAL STACK 50 3.9 490 6.5 4658.9 stack
47

Operating Scenario: OS —22 Emission Source/Group ID: ES-8
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
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%
010 O10 010 010
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
2010
Carbon Dioxide 124389 14050.52 09
CO2
Methane CH4 74-82-8 0.265 09
Nitrous Oxide N20 10024972 0.0265 09
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)
2010
CO CO 9.82 09
NOx NOx 11.69 09
TSP TSP 0.89 09
PM10 PM10 0.67 09
PM2.5 PM2.5 0.22 09
S02 S02 0.07 09
VOC VOC 0.64 09
HAP/TAP Emissions Emission Control
CAS Estimation Efficiency Emission
Pollutants (In CAS EF Control
Alphabetical Order)
(see instructions) (Pounds Year) Method Code (Net after all Factor See Instructions controls)
2010
Benzene 71-43-2 0.491 09
Formaldehyde 50-00-0 17.5 09
Hexane, n— 110-54-3 421 09
48

As entered in AFRO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit: 03085
Lewiston,NC 27849 County : Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
1. Emission Source ID(from permit)or ES-8
Emission Source Group ID
2. Emission Source Description: One natural gas/saleable animal fat/No.6 oil—fired boiler(84 million Btu per
hour maximum heat input capacity)
3. Operating Scenario ID/Description: OS—23/natural gas/saleable animal fat/no.6 oil fired boiler(84 million Btu per
hour heat input)
4. SCC Number/Description: 1020040 1/Residual Oil(No.6)
5. Throughput/units in 2010: 41077 GAL/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) ro
Sulfur 1.8 /o Ash Heat Content 150000 Btu/gallon
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--1? CD-1 OF One packed bed scrubber(288 to 575 gallon per minute normal operating
ange)utilizing water,air,and filter media to reduce PM and S02 emissions
in the boilers and also used conditionally for additional control of
noncondensibles depending on fuel fired in the boilers for the poultry
processing equipment
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-9 VERTICAL STACK 50 3.9 490 6.49 1 4658.9 stack
49

Operating Scenario: OS—23 Emission Source/Group ID:ES-8
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
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 ° arch—May o une—Aug. 25% �010
ept.—Noy. 25%
010 25�° 010 25�° �010
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
2010
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)
2010
CO CO 0.1 08 0
NOx NOx 1.13 08 0
TSP TSP 0.43 02 0.94 AFTER
PM10 PM10 0.4 08 0
PM2.5 PM2.5 0.03 08 0
S02 S02 5.67 02 0.7 AFTER
VOC VOC 0.01 08 0
HAP/TAP Emissions Emission Control Emission
Pollutants (In CAS HAP/TAPS Estimation Efficiency EF Control
(see instructions) Method Code
Alphabetical Order) (Pounds/Year) (Net after all controls) Factor
See Instructions
2010
50

As entered in AERO
Facility Name: Perdue Farms Inc-Lewiston Facility ID : 0800081
3539 Governors Road Permit: 03085
Lewiston,NC 27849 County :Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory-Calendar Year 2010
1. Emission Source ID(from permit)or ES-9
Emission Source Group ID
2. Emission Source Description: One natural gas/saleable animal fat/No.6 oil-fired boiler(84 million Btu per
hour maximum heat input capacity)
3. Operating Scenario ID/Description: OS-24/natural gas/saleable animal fat/no.6 oil fired boiler(84 million Btu per
hour heat input)
4. SCC Number/Description: 1020040 1/Residual Oil(No. 6)
5. Throughput/units in 2010: 41077 GAL/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur 1.8 /o Ash Heat Content 150000 Btu/gallon
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information
Order CS-ID CD ID Control Device Description
as listed inpermit)
1 CS-17 CD-10F One packed bed scrubber(288 to 575 gallon per minute normal operating
ange)utilizing water,air,and filter media to reduce PM and S02 emissions
in the boilers and also used conditionally for additional control of
noncondensibles depending on fuel fired in the boilers for the poultry
processing equipment
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)
EP-9 IVERTICAL STACKF 50 1 3.9 490 1 6.49 1 4658.9 stack
51

Operating Scenario: OS—24 Emission Source/Group ID:ES-9
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
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 arch—May 25% une—Aug. 25% Sept.—nog. 25°��
O10 O10 010 010
13. Actual Emissions per Pollutant Listed
Attach calculations and documentation of emission factors or other estimation methods used.
Emissions— Emission Control
GHG CASGHG Estimation Efficiency Emission Ef Control
Pollutants Pollutants Method Code (Net after Factor
Tons/Year See Instructions) all controls
2010
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)
2010
CO CO 0.1 08 0
NOx NOx 1.13 08 0
TSP TSP 0.43 02 0.94 AFTER
PM10 PM10 0.4 08 0
PM2.5 PM2.5 0.03 08 0
S02 S02 5.67 02 0.7 AFTER
VOC VOC 0.01 08 0
HAP/,TAP Emission
Emissions Control Emission
CAS Estimation EF Control
Pollutants (In HAP/TAPS Efficiency
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2010
52

As entered in AFRO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit: 03085
Lewiston,NC 27849 County : Bertie
DAQ Region :WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
1. Emission Source ID(from permit)or ES-9
Emission Source Group ID
2. Emission Source Description: One natural gas/saleable animal fat/No.6 oil—fired boiler(84 million Btu per
hour maximum heat input capacity)
3. Operating Scenario ID/Description: OS—25/natural gas/saleable animal fat/no.6 oil fired boiler(84 million Btu per
hour heat input)
4. SCC Number/Description: 10200602/Natural Gas
5. Throughput/units in 2010: 233.86 E6FT3/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content 1020 Btu/CF
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-9 IVERTICAL STACK 1 50 1 3.9 490 1 6.49 1 4658.9 stack
53

Operating Scenario: OS—25 Emission Source/Group 1D: ES-9
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
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 ° arch—May ° une—Aug. 25°�° Sept.—Nov. 25'%,
010 25�0 O10 25�O 010 010
13. Actual Emissions ter 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
2010
Carbon Dioxide 124389 14050.52 09
CO2
Methane CH4 74-82-8 0.265 09
Nitrous Oxide N20 10024972 0.0265 09
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)
2010
CO CO 9.82 09
NOx NOx 11.69 09
TSP TSP 0.89 09
PM10 PM10 0.67 09
PM2.5 PM2.5 0.22 09
S02 S02 0.07 09
VOC VOC 0.64 09
HAP/TAP Emissions Emission Control
CAS HAP/.TAPS Estimation Efficiency Emission EF Control
Alphabetical Orde Pollutants (see instructions) Method Code (Net after all Factor
der) (Pounds/Year)
See Instructions controls)
2010
Benzene 71-43-2 0.491 09
Formaldehyde 50-00-0 17.5 09
Hexane n— 110-54-3 421 09
54

As entered in AERO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit: 03085
Lewiston,NC 27849 County : Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
1. Emission Source ID(from permit)or I—ES-6
Emission Source Group ID
2. Emission Source Description: Refrigeration system
3. Operating Scenario ID/Description: OS—26/refrigeration system
4. SCC Number/Description: 39092055/Fuel Storage—Pressure Tanks
5. Throughput/units in 2010: 13758 LB/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 I ERP Information: Sources vented to more than one ERP use additional entry tines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-6 FUGITIVE(NO 1 60 Area= 1 refrigeration
STACK
55

Operating Scenario: OS —26 Emission Source/Group ID: I—ES-6
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
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% �010
ept.—Nov. 25%
2010 010 �010
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
2010
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)
2010
CO CO 08
NOx NOx 08
TSP TSP 08
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP Emissions Emission Control
CAS Efficiency Emission EF Control
Pollutants (In HAP/TAPS Estimation E
(see instructions) Method Code (Net after all Factor
Alphabetical Order) (Pounds/Year) See Instructions controls)
2010
Ammonia(as 7664-41-7 13758 03
NH3
56

As entered in AFRO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit: 03085
Lewiston,NC 27849 County : Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
1. Emission Source ID(from permit) or I—ES-7
Emission Source Group ID
2. Emission Source Description: Propane—fired Singers for singeing poultry
3. Operating Scenario ID/Description: OS—27/propane—fired Singers for singeing poultry
4. SCC Number/Description: 10201002/Liquified Petroleum Gas(LPG)
5. Throughput/units in 2010: 176982 GAL/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) ro
Sulfur /o Ash Heat Content 91000 Btu/gallon
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
LP-7 FUGITIVE(NO 1 60 Area= 1 singers
STACK
57

Operating Scenario: OS—27 Emission Source/Group ID: I—ES-7
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
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 ° y arch—Ma une—Aug. Sept.—Nov. °
010 25�° 010 25% �010 25% O10 25
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 Ef Control
Pollutants CAS Pollutants Method Code (Net after Factor
Tons/Year See Instructions all controls
2010
Carbon Dioxide 124389 1130.38 08
CO2
Methane CH4 74-82-8 0.0538 08
Nitrous Oxide N20 10024972 0.0108 08
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)
2010
CO CO 0.66 09
NOx NOx 1.15 09
TSP TSP 0.06 09
PM10 PM10 0.06 09
PM2.5 PM2.5 0.06 09
S02 S02 0 08
VOC VOC 0.09 09
HAP/TAP Emissions Emission Control
Pollutants (In CAS HAP/TAPS Estimation Efficiency Emission EF Control
Alphabetical Order)
(see instructions) (Pounds/Year) Method Code (Net after all Factor
See Instructions controls)
2010
58

As entered in AER®
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit : 03085
Lewiston,NC 27849 County : Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
1. Emission Source ID (from permit) or I—WWTP
Emission Source Group ID
2. Emission Source Description: Wastewater Treatment System
3. Operating Scenario ID/Description: OS—37/Wastewater Treatment System
4. SCC Number/Description: 30203801/Animal/Poultry Rendering
5. Throughput/units in 2010: 302348 E6GAL/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9. Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
(in 0.1 feet)
WWTP FUGITIVE (NO 1 72 Area— 1 Wastewater Treatment
STACK Operations
59

Operating Scenario: OS—37 Emission Source/Group ID: I—WWTP
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
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% ept.—Nov. 25%
O10 010 �010 O10
13. Actual Emissions Rer 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
2010
Methane CH4 74-82-8 381 03
Criteria Emissions— Emission Control
(NAAQS) Pollutant Criteria Estimation Efficiency Emission Ef Control
Code Pollutants Method Code (Net after Factor
Pollutants (Tons/Year) (See Instructions) all controls)
2010
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 Pollutants (in CAS HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code (Net after all Factor
Alphabetical Order) (Pounds/Year) See Instructions) controls)
2010
60

As entered in AERO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit: 03085
Lewiston,NC 27849 County : Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
1. Emission Source ID(from permit)or IES17
Emission Source Group ID
2. Emission Source Description: Poultry meal conveyance system
3. Operating Scenario ID/Description: OS—33/poultry meal conveyance system
4. SCC Number/Description: 30203805/Animal/Poultry Rendering
5. Throughput/units in 2010: 48026 TON/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur /o Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-17 IVERTICAL STACK 6 0.42 130 1 59.5 494.6 stack
61

Operating Scenario: OS—33 Emission Source/Group ID: IES17
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2010)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start& End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec o o une—Aug. o ept.—Nov. o
2010 25/0 �arch—May
10 25/o )10 25/0 �010 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
2010
Emissions— Emission Control
Criteria Pollutant Criteria Estimation Efficiency Emission
(NAAQS) Ef Control
Code Pollutants Method Code (Net after Factor
Pollutants (Tons/Year) (See Instructions) all controls)
2010
CO CO 08
NOx NOx 08
TSP TSP 6.48 08 0.27
PM10 PM10 08
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP Emission
Emissions Control Emission
CAS HAP/TAPS Estimation Efficiency EF Control
Alphabetical Order) (Pounds/Year) (Net after all controls)
Pollutants (see instructions) Method Code Factor
Order)
See Instructions
2010
62

Facility Total CY 2010 Emissions Summary
As entered in HERO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit: 03085
Lewiston,NC 27849 County : Bertie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2010
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 2010 2009 %Difference
Carbon Dioxide CO2 124389 40995.56 42990.38 —4.6401553%
Methane CH4 74-82-8 381.8205 382.0154 —0.051023014%
Nitrous Oxide 20 10024972 0.0883 .1369 —35.500366%
Criteria Pollutants
Actual Emissions Tons/Year
Pollutant CAS 2010 2009 %Difference
CO CO 30.3 28.26 7.2186804%
NOx NOx 42.81 53.69 —20.264477%
PM TSP TSP 16.57 21.67 —23.534842%
PM10 PM10 9.42 12.61 —25.29738%
PM2.5 PM2.5 0.98 5.02 —80.47809%
S02 S02 11.68 108.1 —89.19519%
VOC VOC 12.08 12.13 —0.41220272%
Hazardous Air Pollutants HAPS and/or Toxic Air Pollutants TAPs
Actual Emissions Pounds/Year
Pollutant I CAS 1 2010 2009 % Difference
Pollutant Grou :Antimon Com ounds total mass,inc elemental SB Grou Sum:0.0
Antimony Unlisted Compounds SBC—Other 0.0 3.4328 —100.0%
(Specify Component of SBC
Pollutant Grou :Arsenic Compounds total mass of elemental AS, arsine and all inorganic compounds) Group Sum:0.0
Arsenic Unlisted Compounds( ASC—Other 0.0 .8631 —100.0%
Specify Component of ASC
Pollutant Group:Beryllium.com ounds Total mass Group Sum:0.0
Beryllium Compound,Unlisted BEC—Other 0.0 .01818 —100.0%
(Specify Component of BEC
Pollutant Grou :Cadmium compounds total mass inc elemental metal Group Sum:0.0
Cadmium Unlisted Compounds CDC—Other 0.0 .26024 —100.0%
(Specify Component of CDC
Pollutant Grou :Cobalt compounds Group Sum:0.0
63

_f
Cobalt Unlisted Compound COC-Other 0.0 3.93628 -100.0%
(Specify Component of COC
ollutant Grou :Lead and Lead compounds Group Sum:0.0
Lead Unlisted Compounds PBC-Other 0.0 .98734 -99.99999%
(Specify and Component of PBC
ollutant Grou :Man anese compounds Group Sum:0.0
Manganese Unlisted Compounds MNC-Other 0.0 1.9616 -100.0%
(Specify Component of MNC
Pollutant Group:Mercury Compounds-all total mass in Hg Vapor Grou Sum:0.0
Mercury Unlisted Compounds HGC-Other 0.0 .07388 -100.0%
(Specify Component of HGC
ollutant Grou :Nickel Compounds sum total mass inc elemental Group Sum:0.0
Nickel Unlisted Compounds NIC-Other 0.0 55.25168 -100.0%
(Specify Component of NIC
ollutant Grou :Chromium(VI) on-Specific Com ounds,as Chrom VI (Co m onent CRC Group Sum:0.0
Chromium(VI)Non-Specific,
Unlisted(Specify Component of NSCR6-Other 0.0 .55252 -100.0
NSCR6 CRC
Pollutant Grou :Chromium-Al otal Inc Chromium VI categories,metal and Others Group Sum:0.0
Chromium(VI)Non-Specific,
Unlisted(Specify Component of NSCR6-Other 0.0 .55252 -100.0%
NSCR6 CRC
ollutant Grou :Pol c clic Or anic Matter(Specific Compounds from OA PS for T Group Sum:.61121
Benzo(a)pyrene(Component of 50-32-8 0.00121 .00139 -12.949638%
POMTV POM7
Naphthalene(Component of 91-20-3 0.61 1.44886 -57.897934%
POMTV)
ollutant Grou :Pol c clic Or anic Matter 7 PAH Com ounds for NIF Grou Sum:.00121
Benzo(a)pyrene(Component of 50-32-8 0.00121 .00139 -12.949638%
POMTV POM7
Acetaldehyde 75-07-0 0.118 .136 -13.235298%
Acrolein 107-02-8 0.037 .043 -13.95349%
Ammonia as NH3 7664-41-7 13758.0 22169 -37.94037%
Benzene 71-43-2 4.98 5.53392 -10.009538%
Ethyl benzene 100-41-4 0.0 .04158 -100.0%
Fluorides(sum of all fluoride 16984-48-8 0.0 24.3892 -99.99999%
compounds)
Formaldehyde 50-00-0 49.58 71.0893 -30.256731%
Hexane,n- 110-54-3 1183.0 1027.3 15.156229%
Methyl chloroform 71-55-6 0.0 .15432 -100.0%
Phosphorus Metal,Yellow or 7723-14-0 0.0 6.18558 -100.0%
White
Polycyclic Organic Matter(Inc
PAH,dioxins,etc.NC AP 42 POM 1.0 1.92464 -48.042233%
historic amorphous lob
Selenium Compounds SEC 0.0 .4466 -100.0%
Toluene 108-88-3 1.32 5.57396 -76.31845%
X lene,o- 95-47-6 0.9 1.11128 -19.01231%
64

As entered in AFRO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit : 03085
Lewiston,NC 27849 County :Bertie
DAQ Region : WARO
Comments From Facility:
65

Emissions by Operating Scenario for Pollutant
2010 Inventory
Facility Name: Perdue Farms Inc—Lewiston
Facility ID : 0800081 Permit : 03085
Process ID Operating Scenario Emission Rate(Tons/Yr)Emission Source ID
Carbon Dioxide CO2
7 propane—fired Singers for singeing oul 1130.38 —ES-7
8 One No. 6 fuel—oil/natural gas—fired boiler(20.3 940.71 S-4
million Btu per hour maximum heat input
6 Generator for Emergency Power/Peak Shaving 190 S-22B
One natural gas—fired temporary,back—up boiler
0 less than 90 million Btu per hour maximum heat 3502.72 S-23
input capacity) SPS Subpart Dc
o. 6 fuel—oil fired boilers(20.3 million Btu per S-4
our heat input)
5natural gas/saleable animal fat/no.6 oil fired boiler 14050.52 S-9
84 million Btu per hour heat input)
5 Generator for Emergency Power/Peak Shaving 190 S-22A
1 One natural gas—fired temporary,back—up boiler S-24
less than 90 million Btu per hour maximum heat
2 natural gas/saleable animal fat/no.6 oil fired boiler 14050.52 S-8
84 million Btu per hour heat input)
One No. 6 fuel—oil/natural gas—fired boiler(20.3
9 million Btu per hour maximum heat input
940.71 S-5
o. 6 fuel—oil fired boilers(20.3 million Btu per
our heat input) S-5
Methane WH4
8 One No. 6 fuel—oil/natural gas—fired boiler(20.3 0743 S-4
million Btu per hour maximum heat input
6 Generator for Emergency Power/Peak Shaving .011 S-22B
o. 6 fuel—oil fired boilers(20.3 million Btu per S-4
our heat input)
35 Generator for Emergency Power/Peak Shaving .011 S-22A
37 Wastewater Treatment System 381 —WWTP
39 One No. 6 fuel—oil/natural gas—fired boiler(20.3 0743 S-5
million Btu per hour maximum heat input
atural gas/saleable animal fat/no.6 oil fired boiler .
5 84 million Btu per hour heat input) 265 S-9
1 One natural gas—fired temporary,back—up boiler S-24
less than 90 million Btu per hour maximum heat
22natural gas/saleable animal fat/no.6 oil fired boiler.265 S-8
84 million Btu per hour heat input)
0 One natural gas—fired temporary,back—up boiler .0661 S-23
less than 90 million Btu per hour maximum heat
1

input capacity) SPS Subpart Dc
5 o. 6 fuel—oil fired boilers(20.3 million Btu per S-5
our heat input)
7 propane—fired Singers for singeing oul .0538 —ES-7
Nitrous Oxide 20
ne natural gas—fired temporary,back—up boiler
0 less than 90 million Btu per hour maximum heat .0066 5-23
n ut capacity) SPS Subpart Dc
7 ro ane—fired Singers for singeing oul .0108 —ES-7
5 Penerator for Emergency Power/Peak Shaving .0016 S-22A
o. 6 fuel—oil fired boilers(20.3 million Btu per S-4
our heat input)
natural gas/saleable animal fat/no.6 oil fired boiler
5 84 million Btu per hour heat input) .0265 S-9
1 ne natural gas—fired temporary,back—up boiler 5-24
less than 90 million Btu per hour maximum heat
2 atural gas/saleable animal fat/no.6 oil fired boiler .0265 S-8
84 million Btu per hour heat input)
36 jenerator for Emergency Power/Peak Shaving .0015 S-22B
39 ne No. 6 fuel—oil/natural gas—fired boiler(20.3 .0074 S-5
illion Btu per hour maximum heat input
38 ne No. 6 fuel—oil/natural gas—fired boiler(20.3 .0074 S-4
million Btu per hour maximum heat input
5 o.6 fuel—oil fired boilers(20.3 million Btu per S-5
our heat input)
CO
9 One No. 6 fuel—oil/natural gas—fired boiler(20.3 2.75 S-5
million Btu per hour maximum heat input
18 _poultry meal storage silo S-15
0 cookers l0A and 10B S-10BES-10A.1
19 Ilive poultry receiving and handling system S-1
1 live poultry receiving and handling system S-3
9 _poultry meal storage silo S-13
3 _poultry meal conveyance system IES17
o. 6 fuel—oil fired boilers(20.3 million Btu per S-4
our heat input)
natural gas/saleable animal fat/no.6 oil fired boiler
5 84 million Btu per hour heat input) 82 S-9
One natural gas—fired temporary,back—up boiler
0 less than 90 million Btu per hour maximum heat 2.45 S-23
input capacity) SPS Subpart Dc
22 natural gas/saleable animal fat/no.6 oil fired boiler 9.82 S_8
84 million Btu per hour heat input)
natural gas/saleable animal fat/no.6 oil fired boiler.
3 84 million Btu per hour heat input) 1 S-8
natural gas/saleable animal fat/no.6 oil fired boiler.
4 84 million Btu per hour heat input) 1 S-9
31process room air collection S—lOD
34 S-19
2

oultry meal loadout area(54 tons per hour
a aci
I ne natural gas—fired temporary,back—up boiler S-24
less than 90 million Btu per hour maximum heat
17 poultry meal storage silo 5-14
26 refrigeration system —ES-6
37 Wastewater Treatment System —WWTP
0 live poultry receiving and handling system S-2
7 propane—fired Singers for singeing oul .66 —ES-7
2 poultry meal storage silo 5-16
5 Generator for Emergency Power/Peak Shaving .93 S-22A
6 Generator for Emergency Power/Peak Shaving .92 S-22B
8 One No.6 fuel—oil/natural gas—fired boiler(20.3 2.75 S-4
billion Btu per hour maximum heat input
o.6 fuel—oil fired boilers(20.3 million Btu per S-5
our heat input)
11 poultry meal storage silo 5-11
15 poultry meal storage silo 5-12
NOx
38 ne No.6 fuel—oil/natural gas—fired boiler(20.3 3.28 S-4
.nillion Btu per hour maximum heat input
39 ne No. 6 fuel—oil/natural gas—fired boiler(20.3 3.28 S-5
llion Btu per hour maximum heat input
18 poultry meal storage silo S-15
30 cookers 1OA and IOB S-10BES-10A.1
19 live poultry receiving and handling system S-1
1 live poultry receiving and handling system S-3
7 propane—fired Singers for singeing oul 1.15 —ES-7
9 poultry meal storage silo S-13
33 _poultry meal conveyance system IES 17
35 Generator for Emergency Power/Peak Shaving S-22A
o. 6 fuel—oil fired boilers(20.3 million Btu per
our heat input) S-4
natural gas/saleable animal fat/no.6 oil fired boiler
4 84 million Btu per hour heat input) 1.13 S-9
31 1process room air collection S-10D
34 poultry meal loadout area(54 tons per hour 5-19
capacity)
36 Generator for Emergency Power/Peak Shaving S-22B
1 One natural gas—fired temporary,back—up boiler 5-24
less than 90 million Btu per hour maximum heat
17 _poultry meal storage silo S-14
natural gas/saleable animal fat/no.6 oil fired boiler 11.69 S-8
84 million Btu per hour heat input)
6 _refrigeration system —ES-6
37 Wastewater Treatment System —WWTP
One natural gas—fired temporary,back—up boiler
0 (less than 90 million Btu per hour maximum heat 1.46 S-23
in ut capacity) SPS Subpart Dc
3

0 _live poultry receiving and handling system S-2
25natural gas/saleable animal fat/no.6 oil fired boiler 11.69 S-9
84 million Btu per hour heat input)
32 poultry meal storage silo S-16
5 o. 6 fuel—oil fired boilers(20.3 million Btu per S-5
our heat input)
11 poultry meal storage silo S-11
15 _poultry meal storage silo S-12
atural gas/saleable animal fat/no.6 oil fired boiler
3 84 million Btu per hour heat input) 1.13 S-8
PM TSP
23 natural gas/saleable animal fat/no.6 oil fired boiler.43 S-8
84 million Btu per hour heat input)
30 cookers l0A and IOB S-10BES-10A.1
36 Generator for Emergency Power/Peak Shaving .12 S-22B
39 ne No. 6 fuel—oil/natural gas—fired boiler(20.3 25 S-5
illion Btu per hour maximum heat input
17 :)oultry meal storage silo 0 ES-14
18 3oultry meal storage silo 0 ES-15
24 natural gas/saleable animal fat/no.6 oil fired boiler .43 S-9
84 million Btu per hour heat input)
o.6 fuel—oil fired boilers(20.3 million Btu per S-4
our heat input)
19 live poultry receiving and handling system 0 S-1
34 poultry meal loadout area(54 tons per hour 6.43 S-19
capacity)
35 Generator for Emergency Power/Peak Shaving .12 S-22A
38 ne No. 6 fuel—oil/natural gas—fired boiler(20.3 .25 S-4
illion Btu per hour maximum heat input
ne natural gas—fired temporary,back—up boiler
0 less than 90 million Btu per hour maximum heat .22 S-23
n ut capacity) SPS Subpart Dc
15 poultry meal storage silo 0 ES-12
9 _poultry meal storage silo 0 ES-13
1 _process room air collection S—lOD
7 Wastewater Treatment System —WWTP
1One natural gas—fired temporary,back—up boiler S-24
less than 90 million Btu per hour maximum heat
1 1 poultry meal storage silo 0 ES-11
0 give poultry receiving and handling system 0 ES-2
1 live poultry receiving and handling system 0 ES-3
6 _refrigeration system —ES-6
5natural gas/saleable animal fat/no.6 oil fired boiler.89 S-9
84 million Btu per hour heat input)
5 o. 6 fuel—oil fired boilers(20.3 million Btu per S-5
our heat input)
natural gas/saleable animal fat/no.6 oil fired boiler .
�284 million Btu per hour heat input) 89 S-8
17 ro ane—fired Singers for singeing oul .06 —ES-7
4

32 kultry meal storage silo 5-16
33 kultry meal conveyance system .48 ES 17
PM 10
natural gas/saleable animal fat/no.6 oil fired boiler .
5 84 million Btu per hour heat input) 67 S-9
30 cookers 10A and IOB S-10BES-10A.1
6 Generator for Emergency Power/Peak Shaving .12 S-22B
17 poultry meal storage silo 0 S-14
18 poultry meal storage silo 0 5-15
33 _poultry meal conveyance system IES17
o. 6 fuel—oil fired boilers(20.3 million Btu per S-4
our heat input)
19 live poultry receiving and handling system 0 S-1
natural gas/saleable animal fat/no.6 oil fired boiler .
3 84 million Btu per hour heat input) 4 S-8
34 poultry meal loadout area(54 tons per hour 6.43 S-19
capacity)
35 Generator for Emergency Power/Peak Shaving .12 S-22A
9 One No. 6 fuel—oil/natural gas—fired boiler(20.3 .19 S-5
million Btu per hour maximum heat input
15 poultry meal storage silo 0 5-12
natural gas/saleable animal fat/no.6 oil fired boiler .
2 84 million Btu per hour heat input) 67 S-8
9 poultry meal storage silo 0 ES-13
31 process room air collection S—lOD
1 One natural gas—fired temporary, back—up boiler S-24
less than 90 million Btu per hour maximum heat
11 poultry meal storage silo 0 ES-11
0 live poultry receiving and handling system 0 ES-2
1 live poultry receiving and handling system 0 S-3
6 _refrigeration system —ES-6
37 Wastewater Treatment System —WWTP
38 One No. 6 fuel—oil/natural gas—fired boiler(20.3 .19 S-4
million Btu per hour maximum heat input
One natural gas—fired temporary,back—up boiler
0 (less than 90 million Btu per hour maximum heat .17 5-23
input capacity) NSPS, Subpart Dc
5 o. 6 fuel—oil fired boilers(20.3 million Btu per S-5
our heat input)
natural gas/saleable animal fat/no.6 oil fired boiler .
4 84 million Btu per hour heat input) 4 S-9
7 ro ane—fired Singers for singeing oul .06 —ES-7
32 _poultry meal storage silo 0 VS-16
PM2.5
18 poultry meal storage silo 5-15
natural gas/saleable animal fat/no.6 oil fired boiler
5 84 million Btu per hour heat input) 22 S-9
30 cookers l0A and IOB S-10BES-10A.1
5

36 Generator for Emergency Power/Peak Shaving .12 S-22B
19 _five poultry receiving and handling system S-1
1 _live poultry receiving and handling system S-3
9 poultry meal storage silo S-13
33 poultry meal conveyance system IES17
38 One No. 6 fuel—oil/natural gas—fired boiler(20.3 .06 S-4
million Btu per hour maximum heat input
o. 6 fuel—oil fired boilers(20.3 million Btu per S-4
our heat input)
3 natural gas/saleable animal fat/no.6 oil fired boiler .03 S-8
84 million Btu per hour heat input)
35 Generator for Emergency Power/Peak Shaving .12 S-22A
39 One No. 6 fuel—oil/natural gas—fired boiler(20.3 .06 S-5
million Btu per hour maximum heat input
One natural gas—fired temporary,back—up boiler
0 less than 90 million Btu per hour maximum heat .06 5-23
input capacity) SPS, Subpart Dc
31 _process room air collection S-101)
34 poultry meal loadout area(54 tons per hour S-19
capacity)
37 Wastewater Treatment System —WWTP
1One natural gas—fired temporary,back—up boiler 5-24
less than 90 million Btu per hour maximum heat
17 poultry meal storage silo S-14
natural gas/saleable animal fat/no.6 oil fired boiler.
2 84 million Btu per hour heat input) 22 S-8
6 refrigeration system —ES-6
0 live poultry receiving and handling system S-2
32 poultry meal storage silo 5-16
5 o. 6 fuel—oil fired boilers(20.3 million Btu per S-5
our heat input)
11 _poultry meal storage silo 5-11
15 _poultry meal storage silo S-12
natural gas/saleable animal fat/no.6 oil fired boiler .
4 84 million Btu per hour heat input) 03 S-9
7 ro ane—fired Singers for singeing oul .06 —ES-7
SO2
18 _poultry meal storage silo S-15
natural gas/saleable animal fat/no.6 oil fired boiler
3 84 million Btu per hour heat input) 5.67 S-8
natural gas/saleable animal fat/no.6 oil fired boiler
5 84 million Btu per hour heat input) 07 S-9
0 cookers l0A and IOB S-10BES-10A.1
19 ive poultry receiving and handling system S-1
1 _live poultry receiving and handling system S-3
9 poultry meal storage silo S-13
3 poultry meal conveyance system IES17
6 Generator for Emergency Power/Peak Shaving .07 S-22B
o. 6 fuel—oil fired boilers(20.3 million Btu per S-4
6

our heat input)
7 ine
o ane—fired Sin ers for sin ein oul —ES-7
8 No. 6 fuel—oil/natural gas—fired boiler(20.3 02 S-4
illion Btu per hour maximum heat input
39 One No. 6 fuel—oil/natural gas—fired boiler(20.3
million Btu per hour maximum heat input
02 S-5
22natural gas/saleable animal fat/no.6 oil fired boiler .07 S-8
84 million Btu per hour heat input)
natural gas/saleable animal fat/no.6 oil fired boiler
�484 million Btu per hour heat input) 5.67 S-9
31 _process room air collection S-10D
34 poultry meal loadout area(54 tons per hour 5-19
a aci
5 jenerator for Emergency Power/Peak Shaving .07 S-22A
ne natural gas—fired temporary,back—up boiler
0 less than 90 million Btu per hour maximum heat .02 5-23
n ut capacity) SPS, Subpart Dc
1One natural gas—fired temporary,back—up boiler 5-24
less than 90 million Btu per hour maximum heat
17 _poultry meal storage silo 5-14
6 reffigeration system —ES-6
7 Wastewater Treatment System —WWTP
0 live poultry receiving and handling system S-2
2 _poultry meal storage silo S-16
5 o.6 fuel—oil fired boilers(20.3 million Btu per S-5
ItIour heat input)
11 bultry meal storage silo S-11
15 oultry meal storage silo 5-12
VOC
18 _poultry meal storage silo S-15
natural gas/saleable animal fat/no.6 oil fired boiler.
3 84 million Btu per hour heat input) O1 S-8
31 _process room air collection 1 S-10D
35 Generator for Emergency Power/Peak Shaving .11 S-22A
One natural gas—fired temporary,back—up boiler
0 less than 90 million Btu per hour maximum heat .16 S-23
input capacity) SPS Subpart Dc
19 live poultry receiving and handling system S-1
1 _live poultry receiving and handling system S-3
9 poultry meal storage silo S-13
3 _poultry meal conveyance system IES17
o. 6 fuel—oil fired boilers(20.3 million Btu per
our heat input) S-4
natural gas/saleable animal fat/no.6 oil fired boiler.
4 84 million Btu per hour heat input) O1 S-9
38 One No. 6 fuel—oil/natural gas—fired boiler(20.3 18 S-4
million Btu per hour maximum heat input
30 cookers l0A and IOB .87 S-10BES-10A.1
36 Generator for Emergency Power/Peak Shaving 11 S-22B
7

25 natural gas/saleable animal fat/no.6 oil fired boiler.
84 million Btu per hour heat input) 64 S-9
27 _pro pane—fired Singers for singeing oul .09 —ES-7
34 poultry meal loadout area(54 tons per hour 5-19
a aci
39 ne No. 6 fuel—oil/natural gas—fired boiler(20.3 .16 S-5
illion Btu per hour maximum heat input
1 ne natural gas—fired temporary,back—up boiler 5-24
Elastewater
ss than 90 million Btu per hour maximum heat
17 ul meal story a silo S-14
6 fri eration system —ES-6
7 Treatment System —WWTP
0 ive poultry receiving and handling system S-2
2 )oultry meal storage silo S-16
5 o.6 fuel—oil fired boilers(20.3 million Btu per S-5
our heat input)
11 3oultry meal storage silo S-11
15 3oultry meal storage silo S-12
atural gas/saleable animal fat/no.6 oil fired boiler
�2 84 million Btu per hour heat input) 64 S-8
Process ID Operating Scenario Emission Rate(Pounds/Yr)Emission Source ID
Acetaldeh de
6 enerator for Emergency Power/Peak Shaving .059 S-22B
5 [Generator for Emergency Power/Peak Shaving .059 S-22A
Acrolein
5 IGenerator for Emergency Power/Peak Shaving .019 S-22A
6 IGenerator for Emergency Power/Peak Shaving .018 S-22B
Ammonia as NH3
6 Ireffigeration system 113758 —ES-6
Antimonv Unlisted Compounds(Specify Component of SBC
o. 6 fuel—oil fired boilers(20.3 million Btu per S-4
our heat input)
o. 6 fuel—oil fired boilers(20.3 million Btu per
our heat input) S-5
Arsenic Unlisted Compounds Specify Component of ASC
o. 6 fuel—oil fired boilers(20.3 million Btu per S-4
our heat input)
o.6 fuel—oil fired boilers(20.3 million Btu per
5 our heat input) S-5
Benzene
ne natural gas fired temporary,back—up boiler
0 less than 90 million Btu per hour maximum heat .122 5-23
n ut ca aci SPS Subpart Del
8

2natural gas/saleable animal fat/no.6 oil fired boiler 491 S-8
84 million Btu per hour heat input)
35 Generator for Emergency Power/Peak Shaving 1.8 S-22A
o. 6 fuel—oil fired boilers(20.3 million Btu per S-4
our heat input)
36 3enerator for Emergency Power/Peak Shaving 1.8 S-22B
39 ne No. 6 fuel—oil/natural gas—fired boiler(20.3 .138 S-5
illion Btu per hour maximum heat input
5 atural gas/saleable animal fat/no.6 oil fired boiler .491 S-9
84 million Btu per hour heat input)
1 ne natural gas—fired temporary,back—up boiler 5-24
less than 90 million Btu per hour maximum heat
38 ne No. 6 fuel—oil/natural gas—fired boiler(20.3 .138 S-4
illion Btu per hour maximum heat input
5Flo. 6 fuel—oil fired boilers(20.3 million Btu per S-5
Itiour heat input)
Benzo a rene(Component of POMTV POM7
5 enerator for Emergency Power/Peak Shavin .00061 S-22A
6 enerator for Emergency Power/Peak Shavin .0006 S-22B
Be Ilium Compound,Unlisted(Specify Component of BEC
o. 6 fuel—oil fired boilers(20.3 million Btu per S-4
our heat input)
5 IN
o. 6 fuel—oil fired boilers(20.3 million Btu per S-5
our heat input)
Cadmium Unlisted Com ounds(Specify Component of CDC
o. 6 fuel—oil fired boilers(20.3 million Btu per S-4
our heat input)
o. 6 fuel—oil fired boilers(20.3 million Btu per
S-5
our heat input)
Chromium VI Non—S ecific Unlisted(Specify Component of NSCR6 CRC
o. 6 fuel—oil fired boilers(20.3 million Btu per S-4
our heat input)
5 o.6 fuel—oil fired boilers(20.3 million Btu per S-5
our heat input)
Cobalt Unlisted Compound(Specify Component of COC
o. 6 fuel—oil fired boilers(20.3 million Btu per S-4
our heat input)
o. 6 fuel—oil fired boilers(20.3 million Btu per S-5
our heat input)
Eth 1 benzene
o. 6 fuel—oil fired boilers(20.3 million Btu per S-4
our heat input)
o.6 fuel—oil fired boilers(20.3 million Btu per S-5
our heat input)
Fluorides(sum of all fluoride compounds)
9

o. 6 fuel—oil fired boilers(20.3 million Btu per S-4
our heat input)
5 o. 6 fuel—oil fired boilers(20.3 million Btu per S-5
our heat input)
Formaldeh de
8 One No.6 fuel—oil/natural gas—fired boiler(20.3 4.92 S-4
million Btu per hour maximum heat input
natural gas/saleable animal fat/no.6 oil fired boiler
5 84 million Btu per hour heat input) 17.5 S-9
o.6 fuel—oil fired boilers(20.3 million Btu per S-4
our heat input)
6 Generator for Emergency Power/Peak Shaving .18 S-22B
natural gas/saleable animal fat/no.6 oil fired boiler
2 84 million Btu per hour heat input) 17.5 S-8
1 [nut
e natural gas—fired temporary,back—up boiler S-24
ss than 90 million Btu per hour maximum heat
35 nerator for Emergency Power/Peak Shaving .19 S-22A
e natural gas—fired temporary,back—up boiler
0 s than 90 million Btu per hour maximum heat 37 5-23
capacity) SPS, Subpart Dc
39 One No. 6 fuel—oil/natural gas—fired boiler(20.3 4.92 S-5
million Btu per hour maximum heat input
5 o.6 fuel—oil fired boilers(20.3 million Btu per ES-5
our heat input)
Hexane n-
39 One No. 6 fuel—oil/natural gas—fired boiler(20.3 118 ES-5
million Btu per hour maximum heat input
1One natural gas—fired temporary,back—up boiler S_24
less than 90 million Btu per hour maximum heat
5natural gas/saleable animal fat/no.6 oil fired boiler 21 S-9
84 million Btu per hour heat input)
2 atural gas/saleable animal fat/no.6 oil fired boiler 21 S-8
84 million Btu per hour heat input)
38 ne No. 6 fuel—oil/natural gas—fired boiler(20.3 118 S-4
illion Btu per hour maximum heat input
Due natural gas—fired temporary,back—up boiler
0 Vput
ess than 90 million Btu per hour maximum heat 105 S-23
capacity) SPS, Subpart Dcl r
Lead Unlisted Compounds(Specify and Component of PBC
o.6 fuel—oil fired boilers(20.3 million Btu per S-4
our heat input)
o.6 fuel—oil fired boilers(20.3 million Btu per
ES-5
our heat input)
Manganese Unlisted Compounds(Specify Component of MNC
o. 6 fuel—oil fired boilers(20.3 million Btu per S-4
our heat input)
o. 6h
uel—oil fired boilers(20.3 million Btu per
our at input) S-5
10

Mercury Unlisted Compounds(Specify Component of HGC
o. 6 fuel—oil fired boilers(20.3 million Btu per ES-4
our heat input)
5 o. 6 fuel—oil fired boilers(20.3 million Btu per S-5
our heat input)
ethyl chloroform
tour
. 6 fuel—oil fired boilers(20.3 million Btu per heat in ut) S-4
5 o. 6 fuel—oil fired boilers(20.3 million Btu per S-5
our heat input)
Na hthalene(Component of POMT
4 Vo. 6 fuel—oil fired boilers(20.3 million Btu per S-4
our heat input)
35 enerator for Emergency Power/Peak Shaving .31 S-22A
36 enerator for Emergency Power/Peak Shaving .3 S-22B
5 o. 6 fuel—oil fired boilers(20.3 million Btu per S-5
our heat input)
Nickel Unlisted Compounds(Specify Com onent of NIC
o.6 fuel—oil fired boilers(20.3 million Btu per S-4
our heat input)
o. 6 fuel—oil fired boilers(20.3 million Btu per S-5
our heat input)
Phos horus Metal Yellow or White
o. 6 fuel—oil fired boilers(20.3 million Btu per S-4
our heat input)
5 o. 6 fuel—oil fired boilers(20.3 million Btu per S-5
our heat input)
Pol c clic Organic Matter Inc PAIL dioxins etc.NC AP 42 historic amorphous lob
tour
.6 fuel—oil fired boilers(20.3 million Btu per S-4
heat input)
6 Generator for Emergency Power/Peak Shaving .5 S-22B
5 Generator for Emergency Power/Peak Shaving .5 S-22A
5 o. 6 fuel—oil fired boilers(20.3 million Btu per S-5
our heat input)
Selenium Com ounds
4 Vo. 6 fuel—oil fired boilers(20.3 million Btu per S-4
our heat input)
5 o.6 fuel—oil fired boilers(20.3 million Btu per S-5
our heat input)
Toluene
o.6 fuel—oil fired boilers(20.3 million Btu per S-4
our heat input)
5 Generator for Emergency Power/Peak Shaving .66 S-22A
6 Generator for Emergency Power/Peak Shaving .66 S-22B
11

o. 6 fuel—oil fired boilers(20.3 million Btu per
S our heat input)
S-5
X lene o-
6 3enerator for Emergency Power/Peak Shaving .45 S-22B
5 jenerator for Emergency Power/Peak Shaving .45 S-22A
o. 6 fuel—oil fired boilers(20.3 million Btu per S-4
our heat input)
o. 6 fuel—oil fired boilers(20.3 million Btu per S-5
our heat input)
12