AQ_F_0800081_20090629_EI_Fac-EI-Rpt

Facility Total CY 2008 Emission Summary Recorded in ED Facility ID #: 0800081
Facility Name: Perdue Farms Inc - Lewiston Permit#(s): 03085T28
Green House Gases Pollutants (GHG) Actual Emissions
Tons/Yr % Difference
Pollutant CAS CY 2008 CY 2007
from ED from Fees
Methane (CH4) 74-82-8 381.72 Not N/A
Reported
Carbon Dioxide (CO2) 124389 46,777.45 Not N/A
Reported
Nitrous Oxide (N20) 10024972 0.614900 Not N/A
Reported
CO2 equivalent(sum of individual GHG pollutant emission times their 49,881.71 metric tons
1995 IPCC Global Warming Potential (GWP), converted to metric tons)
Criteria Pollutants Actual Emissions % Difference
(Tons/Year)
Pollutant CAS CY 2008 CY 2007
from ED from Fees
CO co 26.20 12.59 108.1 %
NOx Nox 66.29 125.01 -47.00%
PM(TSP) TSP 20.92 42.31 -50.6°lo
PM10 PM10 18.10 36.71 -50.7`,
PM2.5 PM2.5 7.35 15.55 -52.7%
S02 S02 166.31 336.95 -50.60%
VOC voc 12.70 34.51 -63.2%
Hazardous Air Pollutants (HAPs) Actual Emissions OX, Difference
and/or Toxic Air Pollutants (TAPs) (Pounds/Year)
Pollutant CAS CY 2008 CY 2007
from ED t from Fees
Polycyclic Organic Matter(Specific Compounds from OAQPS for 1.93 5.42 -64.401's;
To
Benzo(a)pyrene (Component of 833291POMTV& 50-32-8 0.001150 0.001280 N/A
5655317PAH)
Naphthalene (Component of 833291POMTP9 91-20-3 1.93 5.42 -64.4%
Polycyclic Organic Matter(7 PAH Compounds for NIF) 0.001150 0.001280 N/A
WaRO Copy
10/01/2009 Page 1 of 4

Facility Total CY 2008 Emission Summary Recorded in ED Facility ID #: 0800081
Facility Name: Perdue Farms Inc -Lewiston Permit#(s): 03085T28
Hazardous Air Pollutants (HAPs) Actual Emissions % Difference
and/or Toxic Air Pollutants (TAPs) (Pounds/Year)
Pollutant CAS CY 2008 CY 2007
from ED from Fees
Polycyclic Organic Matter (7 PAH Compounds for NIF) 0.001150 0.001280 N/A
Benzo(a)pyrene (Component of 833291POMTV& 50-32-8 0.001150 0.001280 N/A
5655317PAH)
Nickel& Compounds, sum total mass includes elemental 89.61 230.40 -61.1 0
Nickel Unlisted Compounds (Component of NIC- N1C-other 89.61 230.40 -61.1'%o
Specify)
Mercury& Compounds-all total mass includes Hg Vapor 0.134860 0.475680 -71.6?/0
Mercury Unlisted Compounds -Specify Compound HGC-Other 0.134860 0.475680 -71.6%,
(Component of HGC)
Manganese & compounds 3.18 8.18 -61.1
Manganese Unlisted Compounds-Specify MNC-Other 3.18 8.18 -61.1`%
Compound(Component of MNC)
Lead& compounds 1.60 4.12 -61.2%
Lead Unlisted Compounds -Specify Compound PBC-other 1.60 4.12 -61.1'%
(Component of PBC)
Cobalt& compounds 6.38 16.41 -61.1%
Cobalt Unlisted Compounds -Specify Compound COC-other 6.3 8 16.41 -61.1`%
(Component of COC)
Chromium (VI)Non-Specific Compounds, as Chrom(VI) 0.758480 0.770780 -1.6%
(Component CRC)
Chromium (VI)Non-Specific Unlisted Compounds- NSCR6-other 0.758480 0.770780 -1.6%
Specify Compound(Component of NSCR6& CRC)
Chromium-All/Total(includes Chromium (VI) categories, metal 0.896080 2.30 -61.0%
and others
Chromium (VI)Non-Specific Unlisted Compounds- NSCR6-Other 0.758480 0.770780 -1.6%
Specify Compound(Component of NSCR6& CRC)
Chromium Unlisted Compounds-Specify CRC-Other 0.137600 1.5 3 -91.0%
Compound(Component of CRC)
10/01/2009 Page 2 of 4

Facility Total CY 2008 Emission Summary Recorded in ED Facility ID #: 0800081
Facility Name: Perdue Farms Inc - Lewiston Permit#(s): 03085T28
Hazardous Air Pollutants (HAPs) Actual Emissions % Difference
and/or Toxic Air Pollutants (TAPS) (Pounds/Year)
Pollutant CAS CY 2008 CY 2007
from ED from Fees
Cadmium & compounds (total mass includes elemental metal) 0.422040 1.09 -61.3%
Cadmium Unlisted Compounds -Specify Compound CDC-Other 0.422040 1.09 -61.1`%
(Component of CDC)
Beryllium & compounds (Total mass) 0.029480 0.075800 -61.1%
Beryllium Unlisted Compounds -Specify Compound BEC-other 0.029480 0.075800 -6LI0/o
(Component of BEC)
Arsenic & Compounds (total mass of elemental AS, arsine and all 1.40 3.60 -61.1%
inorganic com ounds)
Arsenic Unlisted Compounds -Specify Compound ASC-Other 1.40 3.60 -61.1%
(Component of ASQ
Antimony & Compounds (total mass, inc elemental SB) 5.57 14.32 -61.1%
Antimony Unlisted Compounds -Specify Compound SBC-Other 5.57 14.32 -61.1`%
(Component of SBC)
Acetaldehyde 75-07-0 0.112000 0.127000 -11.8%
Acrolein 107-02-8 0.188000 0.038000 394.7%,
Ammonia(as NH3) 7664-41-7 15,440.00 13,080.00 1.8.0%
Benzene 71-43-2 4.82 4.80 0.3%
Ethyl benzene 100-41-4 0.075900 0.267720 -71.6%
Fluorides (sum of all fluoride compounds as mass of 16984-48-8 44.52 157.01 -71.6`%,
F ion)
Formaldehyde 50-00-0 88.67 179.30 -50.5%,
Hexane, n- 110-54-3 904.00 Not N/A
Reported
Methyl chloroform 71-55-6 0.281680 0.993440 -71.60%
Phosphorus Metal, Yellow or White 7723-14-0 10.03 25.78 -61.1%
Polycyclic Organic Matter(Inc PAH, dioxins, etc. POM 2.21 4.35 -49.1%
NC & AP 42 historic)
10/01/2009 Page 3 of 4

Facility Total CY 2008 Emission Summary Recorded in ED Facility ID #: 0800081
Facility Name: Perdue Farms Inc - Lewiston Permit #(s): 03085T28
Hazardous Air Pollutants (HAPs) Actual Emissions % Difference
and/or Toxic Air Pollutants (TAPs) (Pounds/Year)
Pollutant CAS CY 2008 CY 2007
from ED I from Fees
Selenium Compounds SEC 0.724320 1.86 -61.1%
Toluene 108-88-3 8.65 27.52 -68.60%
Trichloroethane, 1,1,2- 79-00-5 Not Not N/A
Reported Reported
Xylene, o- 95-47-6 0.990100 1.43 -30.7%)
Largest Individual HAP Hexane, n- 904.00 Ibs
Total HAP Emissions 1,033.28 lbs
DAQ's Comments Regarding Inventory
WWTP was new source added for methane. I-ES17 does not have emissions. It is an enclosed operation(a pipe).
Emissions have been incorrectly reported in the past. Formaldehyde,hexane and benzene added for gas combustion.
10/01/2009 Page 4 of 4

r '
1 ,-fps f
6Mr
WaRO Copy
Perdue Farms Incorporated
P.O.Box 460
Lewiston Woodville, NC 27849
www.perdue.com®
Office [phone]
CERTIFIED MAIL 7005 3110 0004 1274 9048 m �.
26-Jun-2009 co d6 ja664,2e
Mr. Robert Fisher, Regional Air Quality Supervisor ��E�/� J�j h°f ha►� �rn1SSS
NCDENR
Division of Air Quality 7 hr d y tTo'm4e'l In�hz
Washington Regional Office
943 Washington Square Mall
Washington, N.C. 27889 U-jlo uJJ" �� 1h&-olt-4Q,P gum
Cor��t ion
Subject: 2008 Emissions Inventory
Perdue Farms Inc.
Cofield. Permit# 02875T23, Facility ID 4600082 ihcfhc ��� '
Lewiston, Permit#03085T27, Facility ID 800081
Dear Mr. Fisher:
Please find enclosed, emission inventory information for the above listed facilities that
were reported online. I have included the following forms for each facility: Aero
Confirmation& Inventory Summary, Certification Form, and spreadsheets for inventory
calculations( CY 2008 ).
I hope this meets with your approval and if you should have any questions regarding this
submittal please contact me at 252-348-4326.
Sincerely,
Wayne Black, REM, REPA
WaRO Copy D Senior Environmental Manager
/enclosures; Air Emission Spreadsheets, Aero Confirmation& Inventory Sum J U N 29 2009
Certification Form
A , DAQ WARO
f-]
A Family commitment to Quality Since 1920'"

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 2008
These forms must be completed and returned even if the facility did not oRmte 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).
ERTIFICATION STATEMENT:
certify that I am the responsible official for this facility,as described above,and hereby certify that the information contained
this air emissions report,including attached calculations and documentation,is true,accurate and complete.(Subject to legal
litics of up to$25,000 per occurrence and possible imprisonment as outlined in G.S.§143-215.3(a)(2))
nsible Official's Signature Below use blue ink): Date Signed:
Name: Wayne Black
OcA
This form applies to Title faciliti f this facility is not classified as Title V,please telephone your regional office Emission
Inventory contact at once for proper forms.
Email address of Responsible Official: [e-mail]
Information on this Form cannot be held confidential
1

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 2008
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).
lERTMICATION STATEMENT:
certify that I am the responsible official for this facility,as described above,and hereby certify that the information contained
enalities
this air emissions report,including attached calculations and documentation,is true,accurate and complete.(Subject to legal
of up to$25,000 per occurrence and possible imprisonment as outlined in G.S.§143-215.3(a)(2))
es onsible Official's Signature Below use blue ink): Date Signed:
d Name: Wayne Black
i ture:
This form applies to Title Vlfacili&ii.44f this facility is not classified as Title V,please telephone your regional office Emission
Inventory contact at once for proper forms.
Email address of Responsible Official: [e-mail]
Information on this Form cannot be held confidential
L
FAQ WA P0 --

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 ED's
Air Permit
ES-1 One live poultry receiving and CS-1 bagfilter(2,100 square feet of filter CD-1
handling system area)
condenser(2488,square feet of
surface area),condenser(2092 square
One poultry by—product cooker feet of surface area) ,condenser(1319 CD—10A.1, CD—10A.2,
and one dual—use square feet of surface area) condenser
ES-10A.1 _ CS I I CD-10A.3,CD-10A.4,
feather/ oult by—product 1183 square feet of surface area
p ry y p ( q )' CD—lOD
cooker 2—stage crossflow wet scrubber(500
gals/min nom. liq. inject.
rate/stage)filter mist eliminator
condenser(2488, square feet of
surface area),condenser(2092 square
feet of surface area) ,condenser(1319 CD—10A.1, CD—10A.2,
ES-1013 poultry by—product presses and CS-11 square feet of surface area) ,condenser CD-10A.3,C13-10A.4,
preheater (1183 square feet of surface area), CD-10D
2—stage crossflow wet scrubber(500
gals/min nom. liq. inject.
rate/sta e)filter mist eliminator
2—stage crossflow wet scrubber(500
ES-10D Process room air collection CS-5 gals/min nom. liq. inject. CD-10D
rate/sta e)filter mist eliminator
ES-11 One poultry meal storage silo CS-8 2 collapsible bagfilters(38 square feet CD-11A,CD-11B
of filter area each)
ES-12 One poultry meal storage silo CS-9 2 collapsible bagfilters(38 square CD-12A,CD-12B
feet of filter area each)
ES-13 One poultry meal storage silo CS-10 2 collapsible bagfilters(38 square CD-13A,CD-13B
feet of filter area each)
ES-14 One poultry meal storage silo CS-12 2 collapsible bagfilters(38 square CD-14A,CD-14B
feet of filter area each)
ES-15 One poultry meal storage silo CS-13 2 collapsible bagfilters(38 square CD—15A,CD—15B
feet of filter area each)
ES-16 One poultry meal storage silo CS-14 2 collapsible bagfilters(38 square CD—16A,CD—16B
feet of filter area each)
ES-19 poultry meal loadout area(54 CS-15 three sided enclosure CD-19(08B)
tons per hour capacity)
ES-2 One live poultry receiving and CS-2 bagfilter(2,100 square feet of filter CD-2
handling system area)
ES-22A
1

One deisel—fired generator
(2628 horsepower engine
output)
One deisel—fired generator
ES-22B (2628 horsepower engine
output)
One natural gas—fired
temporary,back—up boiler(less
ES-23 than 90 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 CD-3
handlings stem area)
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 natural gas/saleable animal venturi wet scrubber(75 gallons per
fat/No.6 oil—fired boiler(84 minute nominal liquid injection rate), CD-10C(08B),CD—lOD,
ES-8 million Btu per hour maximum CS-6 2—stage crossflow wet scrubber(500 CD-1
heat input capacity) gals/min nom. liq. inject.
rate/stage)filter mist eliminator
One natural gas/saleable animal venturi wet scrubber(75 gallons per
fat/No.6 oil—fired boiler(84 minute nominal liquid injection rate), CD-10C(08B),CD—lOD,
ES-9 CS-6 2—stage crossflow wet scrubber(500
million Btu per hour maximum CD-1
heat input capacity) gals/min nom. liq. inject.
rate/stage)filter mist eliminator
I—ES-6 Refrigeration system
I—ES-7 Propane—fired Singers for
singeing poultry
[IE:S7 Poultry 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
DES Group ED *ES ED *OS ED *OS Description
G-31 ES-IOB,ES-10A.1 30 cookers 10A and 10B
ES-1 19 live poultry receiving and handling
system
ES-10D 31 process room air collection
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
ES-23 NONE NONE
ES-3 21 live poultry receiving and handling
system
ES-4 4 No. 6 fuel-oil fired boilers(20.3
million Btu per hour heat input)
ES-5 5 No. 6 fuel-oil fired boilers(20.3
million Btu per hour 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
F S_9 heat input)
natural gas/saleable animal fat/no.6 oil
25 fired boiler(84 million Btu per hour
heat input)
3

I—ES-6 26 refrigeration system
I—ES-7 27 propane—fired Singers for singeing
poultry
IES17 33 poultry 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 2008
1. Emission Source ID(from permit)or Group G-31 consisting of ES—IOB,ES-10A.1
Emission Source Group ID
2. Emission Source Description: cookers IOA and 1 OB
3. Operating Scenario ID/Description: OS—30/cookers IOA and 1 OB
4. SCC Number/Description: 30203803/Animal/Poultry Rendering
5. Throughput/units in 2008: 235206 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-11 CD-1 OA.1 One condenser 2488 square feet of surface area
2 CS-11 CD-10A.2 One condenser 2092 square feet of surface area
3 CS-11 CD-10A.3 One condenser 1319 square feet of surface area
4 CS-11 CD-10A.4 One condenser 1183 square feet of surface area
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 VERTICAL STACKI 62.5 1.18 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 2008)
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 o June-Aug. o ept.—Nov.
008 008 25/0 2008 25/0 �008 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
2008
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po�QS Code Pollutants Method Code Ef Control
Pollutantss (Net after Factor
(Tons/Year) (See Instructions) all controls)
2008
CO CO 08 0
NOx NOz 08 0
TSP TSP 08 0
PM10 PM10 08 0
PM2.5 PM2.5 08 0
S02 S02 08 0
VOC VOC 10.78 09 85 0.0917 AFTER
HAP/TAP Emissions Emission Control
CAS Estimation Emission
Pollutants (in (see instructions) HAP/TAPS Method Code Efficiency Factor EF Control
Alphabetical Order) (Pounds/Year) See Instructions) (Net after all controls)
2008
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
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2008
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 2008: 33156685 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—I 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#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-1 IVERTICAL 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 2008)
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 25p�o arch—May 25"�u une—Aug. 25"�u Sept.—Nov. 25%
2008 008 008 008
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
2008
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po�QS Code Pollutants Method Code (Net after Factor Ef Control
Pollutantss
(Tons/Year) (See Instructions) all controls)
2008
CO CO 08 0
NOz NOz 08 0
TSP TSP 0 09 99.9 0.0003 BEFORE
PM10 PM10 0 09 99.9 0.0003 BEFORE
PM2.5 PM2.5 08 0
S02 S02 08 0
VOC VOC 08 0
HAP/TAP Emissions EmissionControl
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
2008
8

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 2008
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: 30299999/*Other Not Specified
5. Throughput/units in 2008: 235206 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-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#): (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/Group ID: ES-1 OD
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2008)
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. Z>%
008 1 �2O08 �008 008
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
2008
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)
2008
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 0.1 08 85
HAP/TAP Emissions Emission
CAS Estimation Control Emission
Pollutants (In (see instructions) HAP/TAPS Efficiency Factor EF Control
Method Code
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2008
10

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 2008
1. Emission Source ID(from permit)or ES-11
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: 30299999/*Other Not Specified
5. Throughput/units in 2008: 8514 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-11B 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-11 VERTICAL STACK 53 1.18 120 T 7.1 465.86 stack
11

Operating Scenario: OS— 11 Emission Source/Group ID: ES-11
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2008)
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 Through ut:
an—Feb +Dec 25% arch—May 25% une—Aug. 25% Sept.—Nov. 25%
008 2008 008 008
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
2008
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)
2008
CO CO 08 0
NOz NOz 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
See Instructions)
Alphabetical Order) (Pounds/Year) (Net after all controls)
2008
12

As entered in AFRO
Facility Name: Perdue Farms Inc—Lewiston Facility ID : 0800081
3539 Governors Road Permit: 03085
Lewiston,NC 27849 County :Bettie
DAQ Region : WARO
North Carolina Department of Environment and Natural Resources
Division of Air Quality
Air Pollutant Point Source Emissions Inventory—Calendar Year 2008
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: 30299999/*Other Not Specified
5. Throughputlunits in 2008: 8514 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#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-12 VERTICAL STACK 51 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 2008)
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% March—May 25% une—Aug. 25% Sept.—Nov. 25%
008 2008 2008 2008
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
2008
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)
2008
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
Pollutants (In HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2008
14

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 2008
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 lD/Description: OS —29/poultry meal storage silo
4. SCC Number/Description: 30203805/Animal/Poultry Rendering
5. Throughputtunits in 2008: 8514 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—lD CD ID Control Device Description
as listed inpermit)
1 CS-10 CD-13A One collapsible ba filter 38 square feet of filter area
CS-10 CD-13B 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-13 IVERTICAL STACK 53 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 2008)
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% March—May 25% une—Aug. 250�o Sept.—Nov. 25%
2008 2008 2008 2008
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
2008
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAAQS) y Ef Control
Pollutants Code Pollutants Method Code (Net after Factor
(Tons/Year) (See Instructions) all controls)
2008
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
CAS 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
2008
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 2008
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: 30299999/*Other Not Specified
5. Throughputlunits in 2008: 8514 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-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 VERTICAL STACK 51 0.94 120 12.1 503.82 stack
17

Operating Scenario: OS - 17 Emission Source/Group ID: ES-14
P g P
10.Operating Schedule: (Source/Operating eratin Scenario that best characterizes Calendar Year 2008
P g P g )
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 March—May a une—Aug. o Sept.—Nov. o
25/0 25/0 25/0 25/o
2008 2008 �2008 �2008
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
2008
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)
2008
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
Control
Pollutants (In HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2008
18

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 2008
1. Emission Source ED (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: 30299999/*Other Not Specified
5. Throughputlunits in 2008: 8514 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 1.18 120 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 2008)
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% March—May 25% June—Aug. Z5% Sept.—Nov. 25%
2008 2008 2008 008
13. Actual Emissions per Pollutant Listed
Attach calculations and documentationof 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
2008
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAAQS Code Pollutants Method Code (Net after Factor Ef Control
Pollutantss
(Tons/Year) (See Instructions) all controls)
2008
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 (see instructions) HAP/TAPS Efficiency Factor EF Control
Method Code
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2008
20

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 2008
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: OS—32/poultry meal storage silo
4. SCC Number/Description: 30203805/Animal/Poultry Rendering
5. Throughput/units in 2008: 8514 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-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 VERTICAL STACK 53 1.18 120 7.1 465.86 stack
21

Operating Scenario: OS —32 Emission Source/Group ID: ES-16
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2008)
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% March—May 25°�° une—Aug. ° Sept.—Nov. °
2008 2008 2008 25/0 2008 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
2008
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
(NAAQS) y Ef Control
Pollutants Code Pollutants Method Code (Net after Factor
(Tons/Year) (See Instructions) all controls)
2008
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
CAS 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
2008
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 2008
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 2008: 50749 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—El) CD ID Control Device Description
as listed inpermit)
1 CS-15 CD-19 08B three sided enclosure
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/see) (Acfm)
Rectangle(L x W)
in 0.1 feet)
23

Operating Scenario: OS —34 Emission Source/Group ID: ES-19
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2008)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
IL Typical Start& End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
an—Feb +Dec 250o March—May 25% June—Aug. 25% Sept.—Nov. 25%
: 7
2008 2008 2008 2008
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
2008
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)
2008
CO CO 08 0
NOx NOx 08 0
TSP TSP 6.23 08 9 0.27 BEFORE
PM10 PM10 6.23 08 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
2008
24

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 2008
1. Emission Source ID(from permit)or ES-2
Emission Source Group ED
2. Emission Source Description: One live poultry receiving and handling system
3. Operating Scenario 1D/Description: OS—20/live poultry receiving and handling system
4. SCC Number/Description: 30203805/Animal/Poultry Rendering
5. Throughput/units in 2008: 33156685 EACH/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—II) CD ID Control Device Description
as listed inpen-nit)
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 VERTICAL STACK 14.4 1 2.25 60 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 2008)
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%
2008 1 2008 �008 008
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
2008
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po�QS) Code Pollutants Method Code Ef Control
lltt
Pollutants (Net after Factor
(Tons/Year) (See Instructions) all controls)
2008
CO CO 08 0
NOz NOz 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
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
2008
26

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 2008
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. Throughputtunits in 2008: 126 HR/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur 0.05 %Ash Heat Content 139000 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 RP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) (Acfm)
Rectangle(L x W)
(in 0.1 feet)
EP22A FUGITIVE(NO 1 72 Area= 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 2008)
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% March—May 25% une—Aug. 25% Sept.—Nov. 25%
2008 2008 2008 2008
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 (]vet after Factor
Tons/Year See Instructions all controls
2008
Carbon Dioxide CO2 124389 190 08
Methane CH4 74-82-8 0.011 08
Nitrous Oxide 20 10024972 0.0015 08
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)
2008
CO CO 0.91 09
NOx NOx 4 09
TSP TSP 0.12 09
PM10 PM10 0.12 09
PM2.5 PM2.5 0.12 09
S02 S02 0.07 09
VOC VOC 0.12 09
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)
2008
Acetaldehyde 75-07-0 0.058 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
POMTV
Polycyclic Organic Matter (Inc
PAH,dioxins, etc.NC AP 42 POM 0.49 09
historic amorphous lob
28

Toluene 108-88-3 0.65 09
X lene,o— 95-47-6 0.45 09
29

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 2008
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 2008: 116 HR/
Yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) %Sulfur 0.05 %Ash Heat Content 139000 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 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

Operating Scenario: OS—36 Emission Source/Group ID: ES-22B
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2008)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start& End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
Jan—Feb +Dec 25�° March—Ma Se t.—Nov.
2008 ° 2, y 25% �une—Aug.
008 25% 2008 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
2008
Carbon Dioxide CO2 124389 170 08
Methane CH4 74-82-8 0.0097 08
Nitrous Oxide 20 10024972 0.0014 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)
2008
CO CO 0.84 09
NOx NOx 3.7 09
TSP TSP 0.11 09
PM10 PM10 0.11 09
PM2.5 PM2.5 0.11 09
S02 S02 0.06 09
VOC VOC 0.11 09
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)
2008
Acetaldehyde 75-07-0 0.054 09
Acrolein 107-02-8 0.17 09
Benzene 71-43-2 1.7 09
Benzo(a)pyrene(Component of 50-32-8 0.00055 09
POMTV POM7
Formaldehyde 50-00-0 0.17 09
Naphthalene (Component of
91-20-3 0.28 09
POMTV
Polycyclic Organic Matter (Inc
PAH, dioxins, etc. NC AP 42 POM 0.45 09
historic amorphous lob
31

Toluene 108-88-3. 0.6 09
Xylene,o— 95-47-6 0.41 09
32

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 2008
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 2008: 33156685 EACH/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-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 EPP 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-3 VERTICAL STACK 14.4 2.25 60 4.51 1076 stack
33

I
Operating Scenario: OS—21 Emission Source/Group ID: ES-3
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2008)
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 2! une—Aug. 25% Sept.—Nov. 25%
008 2008 0n 008
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
2008
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)
2008
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 '
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
2008
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 2008
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: 10200401/Residual Oil(No. 6)
5. Throughput/units in 2008: 448799 GAL/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) %Sulfur 2.1 /o Ash Heat Content 150000 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)
1- i
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines :
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-4 VERTICAL STACK 20 2 400 19.1 3600.26 stack
35

Operating Scenario: OS—4 Emission Source/Group ID: ES-4
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2008)
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%
008 1 2008 �008 2008
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
2008
Carbon Dioxide CO2 124389 5848.3 08
Methane CH4 74-82-8 0.22 08
Nitrous Oxide 20 10024972 0.02 08
Emissions— Emission Control
Criteria Estimation
(NAAQS) Pollutant Criteria Efficiency Emission
Code Pollutants Method Code (Net after Factor Ef Control
Pollutants (See
(Tons/Year) all controls)
Instructions
2008
CO CO 1.12 09
NOx NOx 12.34 09
TSP TSP 5.39 09
PM10 PM10 4.38 09
PM2.5 PM2.5 2.85 09
S02 S02 73.98 09
VOC VOC 0.06 09
HAP/TAP Emissions Emission Control
CAS Estimation Efficiency Emission
Pollutants (In Alphabetical (see instructions) HAP/TAPS Method Code (Net after all Factor EF Control
Order) (Pounds/Year)
(See Instructions) controls)
2008
Antimony Unlisted
Compounds(Specify SBC—Other 2.35619 08 0.00000525
Component of SBC
Arsenic Unlisted
Compounds(Specify ASC—Other 0.59241 08 0.00000132
Component of ASC
Benzene 71-43-2 0.09604 08 0.000000214
Beryllium Compound,
Unlisted (Specify BEC—Other 0.01248 08 0.0000000278
Component of BEC
CDC—Other 0.17862 08 0.000000398
36

Cadmium Unlisted
Compounds(Specify
Component of CDC
Chromium (VI)
Non-Specific,Unlisted NSCR6-Other 0.37924 08 0.000000845
(Specify Component of
NSCR6 CRC
Cobalt Unlisted Compound
(Specify Component of COC-Other 2.70177 08 0.00000602
COC
Eth 1 benzene 100-41-4 0.02854 08 0.0000000636
Fluorides (sum of all 16984-48-8 16.7402 08 0.0000373
fluoride compounds)
Formaldehyde 50-00-0 19.07396 08 0.0000425
Lead Unlisted Compounds
(Specify and Component of PBC-Other 0.67769 08 0.00000151
PBC
Manganese Unlisted
Compounds (Specify MNC-Other 1.3464 08 0.000003
Component of MNC
Mercury Unlisted
Compounds (Specify HGC-Other 0.05071 08 0.000000113
Component of HGC
Methyl chloroform 71-55-6 0.10592 08 0.000000236
Naphthalene(Component of 91-20-3 0.50714 08 0.00000113
POMTV
Nickel Unlisted Compounds
(Specify Component of NIC-Other 37.92352 08 0.0000845
NIC
Phosphorus Metal,Yellow 7723-14-0 4.24564 08 0.00000946
or White
Polycyclic Organic Matter
(Inc PAH, dioxins,etc.NC POM 0.53856 08 0.0000012
AP 42 historic amorphous
lob
Selenium Compounds SEC 0.30653 08 0.000000683
Toluene 108-88-3 2.78255 08 0.0000062
X lene, o- 95-47-6 0.04892 08 0.000000109
37

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 2008
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 ED/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 2008: 448799 GAL/yr
(e.g.production or fuel use):
6. Fuel Information (if fuel is used) % Sulfur ?.l Asli Heat Content 150000 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 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-5 VERTICAL STACKI 20 2 400 19.1 3600.26 stack
38

Operating Scenario: OS — 5 Emission Source/Group ID: ES-5
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2008)
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% March—May 25% June—Aug. 25% Sept.—Nov. 25%
2008 1 2008 2008 2008
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)
2008
Carbon Dioxide CO2 124389 5848.3 08
Methane CH4 74-82-8 0.22 08
Nitrous Oxide 20 10024972 0.02 08
Emissions— EmissionControl
Criteria Estimation
Pollutant Criteria Efficiency
Emission
(NAAQS) Code Pollutants Method Code (Net after Factor Ef Control
Pollutants (See
(Tons/Year) all controls)
Instructions
2008
CO CO 1.12 09
NOx NOx 12.34 09
TSP TSP 5.39 09
PM10 PM10 4.38 09
PM2.5 PM2.5 2.85 09
S02 S02 73.98 09
VOC VOC 0.06 08
HAP/TAP Emissions Emission Control
Pollutants (In Alphabetical CAS HAP/TAPS Estimation Efficiency Emission EF Control
Order) (Pounds/Year)
(see instructions) Method Code (Net after all Factor
See Instructions controls)
2008
Antimony Unlisted
Compounds (Specify SBC—Other 2.35619 08 0.00000525
Component of SBC
Arsenic Unlisted
Compounds(Specify ASC—Other 0.59241 08 0.00000132
Component of ASC
Benzene 71-43-2 0.09604 08 0.000000214
Beryllium Compound,
Unlisted (Specify BEC—Other 0.01248 08 0.0000000278
Component of BEC
CDC—Other 0.17862 08 0.000000398
39

Cadmium Unlisted
Compounds (Specify
Component of CDC)
Chromium (VI)
Non-Specific, Unlisted NSCR6-Other 0.37924 08 0.000000845
(Specify Component of
NSCR6 CRC
Cobalt Unlisted Compound
(Specify Component of COC-Other 2.70177 08 0.00000602
COC
Eth lbenzene 100-41-4 0.02854 08 0.0000000636
Fluorides (sum of all 16984-48-8 16.7402 08 0.0000373
fluoride compounds)
Formaldehyde 50-00-0 19.07396 08 0.0000425
Lead Unlisted Compounds
(Specify and Component of PBC-Other 0.67769 08 0.00000151
PBC
Manganese Unlisted
Compounds(Specify MNC-Other 1.3464 08 0.000003
Component of MNC
Mercury Unlisted
Compounds(Specify HGC-Other 0.05071 08 0.000000113
Component of HGC
Methvl chloroform 71-55-6 0.10592 08 0.000000236
Naphthalene (Component of 91-20-3 0.50714 08 0.00000113
POMTV
Nickel Unlisted Compounds
(Specify Component of NIC-Other 37.92352 08 0.0000845
NIC
Phosphorus Metal, Yellow 7723-14-0 4.24564 08 0.00000946
or White
Polycyclic Organic Matter
(Inc PAH,dioxins, etc. NC POM 0.53856 08 0.0000012
AP 42 historic amorphous
lob
Selenium Compounds SEC 0.30653 08 0.000000683
Toluene 108-88-3 2.78255 08 0.0000062
Xylene, o- 95-47-6 0.04892 08 0.000000109
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 2008
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 2008: 251 E6FT3S/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /u Sulfur /o Ash Heat Content 1029 Btu/CF
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-6 CD-10C 08B venturi wet scrubber 75 gallons per minute nominal liquid injection rate
2 CS-6 CD-10D One two—stage crossflow wet scrubber(500 gallons per minute nominal
liquid injection rate per stage)and a dry filter mist eliminator
3 CS-6 CD-1 One ba tlter(2,800 square feet of filter area
I
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-9 VERTICAL STACK 50 3.9 490 6,5 4658.9 stack
41

Operating Scenario: OS —22 Emission Source/Group ID: ES-8
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2008)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11. Typical Start& End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
Jan—Feb +Dec 25% March—May 25% une—Aug. 25% Sept.—Nov. 25%
2008 2008 2008 2008
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)
2008
Carbon Dioxide 124389 15105.18 08 0
CO2
Methane CH4 74-82-8 0.256 08 0
Nitrous Oxide 20 10024972 0.256 08 0
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)
2008
CO CO 10.54 08 0
NOx NOx 12.55 08 0
TSP TSP 0.95 08 45
PM10 PM10 0.72 08 0
PM2.5 PM2.5 0.24 08 0
S02 S02 0.08 08 56.8
VOC VOC 0.69 08 0
HAP/TAP Emissions Emission Control
CAS Estimation Efficiency Emission
Pollutants (in (see instructions) HAP/TAPS Method Code (Net after all Factor EF Control
Alphabetical Order) (Pounds/Year)
See Instructions controls)
2008
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 2008
1. Emission Source II)(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: 10200401/Residual Oil(No. 6)
5. Throughput/units in 2008: 147956 GAL/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) ro
Sulfur 1.8 % Asli 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—II) CD ID Control Device Description
as listed inpermit)
1 CS-6 CD-10C 08B venturi wet scrubber 75 gallons per minute nominal liquid injection rate
2 CS-6 CD-10D One two—stage crossflow wet scrubber(500 gallons per minute nominal
liquid injection rate per stage)and a dry filter mist eliminator
3 CS-6 CD-1 One ba filter 2,800 square feet of filter area
9.Emission Release Point RP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ED 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 VERTICALSTACKI 50 1 3.9 490 1 6.5 1 4658.9 1 stack
43

Operating Scenario: OS — 23 Emission Source/Group ID:ES-8
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2008)
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%
008 1 2008 �008 008
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
2008
Carbon Dioxide CO2 124389 1928.01 08 0
Methane CH4 74-82-8 0.07 08 0
Nitrous Oxide 20 10024972 0.01 08 0
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po�QS Code Pollutants Method Code (Net after Factor Ef Control
Pollutantss
(Tons/Year) (See Instructions) all controls)
2008
CO CO 0.37 09
NOx NOx 4.07 09
TSP TSP 0.87 09
PM10 PM10 0.7 09
PM2.5 PM2.5 0.45 09
S02 S02 9.03 09
VOC VOC 0.02 09
HAP/TAP Emissions Emission ControlEmission CAS Estimation Efficiency EF Control
Pollutants (In Alphabetical HAP/TAPS
Order)
(see instructions) (Pounds/Year) Method Code (Net after all Factor
See Instructions controls)
2008
Antimony Unlisted
Compounds(Specify SBC—Other 0.42759 09 45 0.00000289 AFTER
Component of SBC
Arsenic Unlisted
Compounds(Specify ASC—Other 0.10742 09 45 0.000000726 AFTER
Component of ASC
Benzene 71-43-2 0.03166 09 0.000000214
Beryllium Compound,
Unlisted (Specify BEC—Other 0.00226 09 45 0.0000000153 AFTER
Component of BEC
Cadmium Unlisted CDC—Other 0.0324 09 45 0.000000219 AFTER
Compounds(Specify
44

Component of CDC
Chromium Unlisted
Compounds (Specify CRC-Other 0.0688 09 45 0.000000465 AFTER
Component of CRC
Cobalt Unlisted Compound
(Specify Component of COC-Other 0.48973 09 45 0.00000331 AFTER
COC
Eth lbenzene 100-41-4 0.00941 09 0.0000000636
Fluorides (sum of all 16984-48-8 5.51876 09 0.0000373
fluoride compounds)
Formaldehyde 50-00-0 6.28813 09 0.0000425
Lead Unlisted Compounds
(Specify and Component of PBC-Other 0.12295 09 45 0.000000831 AFTER
PBC
Manganese Unlisted
Compounds (Specify MNC-Other 0.24413 09 45 0.00000165 AFTER
Component of MNC
Mercury Unlisted
Compounds (Specify HGC-Other 0.01672 09 0.000000113
Component of HGC
Methyl chloroform 71-55-6 0.03492 09 0.000000236
Naphthalene (Component of 91-20-3 0.16719 09 0.00000113
POMTV
Nickel Unlisted Compounds NIC-Other 6.87995 09 45 0.0000465 AFTER
(Specify Component of NIC
Phosphorus Metal, Yellow 7723-14-0 0.76937 09 45 0.0000052 AFTER
or White
Polycyclic Organic Matter
(Inc PAH, dioxins, etc.NC POM 0.09765 09 45 0.00000066 AFTER
AP 42 historic amorphous
lob
Selenium Compounds SEC 0.05563 09 45 0.000000376 AFTER
Toluene 108-88-3 0.91733 09 0 0.0000062
X lene,o- 95-47-6 0.01613 09 0 0.000000109
45

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 2008
1. Emission Source H) (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 2008: 147956 GAL/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur 1.84 %Ash I 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-6 CD—IOC 08B venturi wet scrubber 75 gallons per minute nominal liquid injection rate
2 CS-6 CD-10D One two—stage crossflow wet scrubber(500 gallons per minute nominal
liquid injection rate per stage)and a dry filter mist eliminator
3 CS-6 CD—I 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-9 IVERTICAL STACKI 50 3.9 490 6.5 4658.9 stack
46
1

Operating Scenario: OS—24 Emission Source/Group ID: ES-9
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2008)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11.Typical Start&End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throughput:
an—Feb +Dec o arch—May ° une—Aug. ° Sept.—Nov. °
2008 25/0 2008 25/° �008 25/° 2008 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
2008
Carbon Dioxide CO2 124389 1928.01 08 0
Methane CH4 74-82-8 0.07 08 0
Nitrous Oxide 20 10024972 0.01 08 0
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)
2008
CO CO 0.37 09
NOx NOx 4.07 09
TSP TSP 0.87 09
PM10 PM10 0.7 09
PM2.5 PM2.5 0.45 09
S02 S02 9.03 09
VOC VOC 0.02 09
RAP/TAP Emissions Emission Control
Pollutants (In Alphabetical CAS HAP/TAPS Estimation Efficiency Emission EF Control
Order) (see instructions) (Pounds/Year) Method Code (Net after all Factor
See Instructions controls)
2008
Antimony Unlisted
Compounds(Specify SBC—Other 0.42759 08 45 0.00000289 AFTER
Component of SBC
Arsenic Unlisted
Compounds(Specify ASC—Other 0.10742 08 45 0.000000726 AFTER
Component of ASC
Benzene 71-43-2 0.03166 08 0.000000214
Beryllium Compound,
Unlisted (Specify BEC—Other 0.00226 08 45 0.0000000153 AFTER
Component of BEC
Cadmium Unlisted CDC—Other 0.0324 08 45 0.000000219 AFTER
Compounds (Specify
47

Component of CDC
Chromium Unlisted
Compounds(Specify CRC-Other 0.0688 08 45 0.000000465 AFTER
Component of CRC
Cobalt Unlisted Compound
(Specify Component of COC-Other 0.48973 08 45 0.00000331 AFTER
COC
Eth 1 benzene 100-41-4 0.00941 08 0.0000000636
Fluorides(sum of all 16984-48-8 5.51876 08 0.0000373
fluoride compounds)
Formaldehyde 50-00-0 6.28813 08 0.0000425
Lead Unlisted Compounds
(Specify and Component of PBC-Other 0.12295 08 45 0.000000831 AFTER
PBC
Manganese Unlisted
Compounds(Specify MNC-Other 0.24413 08 45 0.00000165 AFTER
Component of MNC
Mercury Unlisted
Compounds(Specify HGC-Other 0.01672 08 0.000000113
Component of HGC
Methyl chloroform 71-55-6 0.03492 08 0.000000236
Naphthalene(Component of 91-20-3 0.16719 08 0.00000113
POMT
Nickel Unlisted Compounds NIC-Other 6.87995 08 45 0.0000465 AFTER
(Specify Component of NIC
Phosphorus Metal,Yellow 7723-14-0 0.76937 08 45 0.0000052 AFTER
or White
Polycyclic Organic Matter
(Inc PAH,dioxins,etc.NC POM 0.09765 08 45 0.00000066 AFTER
AP 42 historic amorphous
lob
Selenium Compounds SEC 0.05563 08 45 0.000000376 AFTER
Toluene 108-88-3 0.91733 08 0.0000062
X lene o- 95-47-6 0.01613 08 0.000000109
48

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 2008
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 2008: 251 E6FT3S/yr.
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) ro
Sulfur /o Ash Heat Content 1029 Btu/CF
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control 100
Device or Stack):
8. Control Device Information
Order CS—El) CD ID Control Device Description
as listed inpermit)
I CS-6 CD-10 08B venturi wet scrubber 75 gallons per minute nominal liquid injection rate
CS-6 CD-10D One two—stage crossflow wet scrubber(500 gallons per minute nominal
liquid injection rate per stage)and a dry filter mist eliminator
3 CS-6 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#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
(in 0.1 feet)
EP-9 VERTICAL STACK 50 3.9 490---r 6.5 4658.9 stack
49
i

Operating Scenario: OS —25 Emission Source/Group ID: ES-9
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2008)
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% Sept.—Nov. 25%
008 2008 008 008
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
2008
Carbon Dioxide 124389 15105.18 08 0
CO2
Methane CH4 74-82-8 0.256 08 0
Nitrous Oxide 20) 10024972 0.256 08 0
Criteria Emissions— Emission Control
Pollutant Criteria Estimation Efficiency Emission
Po� Code Pollutants Method Code (Net after Factor Ef Control
Pollutants
(Tons/Year) (See Instructions) all controls)
2008
CO CO 10.54 08 0
NOx NOx 12.55 08 0
TSP TSP 0.95 08 45
PM10 PM10 0.72 08 0
PM2.5 PM2.5 0.24 08 0
S02 S02 0.08 08 56.8
VOC VOC 0.69 08 0
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)
2008
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 2008
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. Throughputlunits in 2008: 15440 LB/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 in perniit)
�--1 I i 1
9.Emission Release Point ERP Information: Sources vented to more than one ERP use additional entry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter ft (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-6 FUGITIVE(NO 1 60 Area I refrigeration
STACK
51

Operating Scenario: OS—26 Emission Source/Group ID: I—ES-6
10.Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2008)
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'Vo �008
ept.—Nov. 25%
008 008 �008
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 ear) See Instructions all controls
2008
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)
2008
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 ControlEmission CAS Estimation Efficiency Pollutants (In HAP/TAPS y EF Control
Alphabetical Order)
(see instructions) (Pounds/Year) Method Code (Net after all Factor
See Instructions controls)
2008
Ammonia(as 7664-41-7 15440 03
NH3
52

As entered in AERO
Facility Name: Perdue Farms Inc—Lewiston Facility ED : 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 2008
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 2008: 103816 GAL/yr
(e.g.production or fuel use):
6. Fuel Information (if fuel is used) goSulfur /oAsh Heat Content 91000 Btivgallon
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack):
8. Control Device Information :None
Order CS—II) CD ED Control Device Description
as listed inpermit)
�__l I i 1
9.Emission Release PoPointERP Informah thann on: Sources vented to more one ERP use additiona entry lines :
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow Rate ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) (Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-7 FUGITIVE(NO 1 60 Area= 1 singers
STACK
53

Operating Scenario: OS — 27 Emission Source/Group ID: I—ES-7
P g P
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2008)
Hours per Day ( 24 ) Days per Week ( 7 ) Weeks per Year ( 52 )
11. Typical Start& End Times For Operating Scenario: Start: 0 End: 2359
12. Seasonal Periods Percent Annual Throu h ut:
Jan—Feb +Dec 25% March—May une—Aug. o Sept.—Nov.
2008 2008 25% 2008 25/0 2008 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
2008
Carbon Dioxide 124389 654.47 08
CO2
Methane CH4 74-82-8 0.01 08
Nitrous Oxide 20 10024972 0.04 08
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)
2008
CO CO 0.39 09
NOx NOx 0.67 09
TSP TSP 0.04 09
PM10 PM10 0.04 09
PM2.5 PM2.5 0.04 09
S02 S02 0 09
VOC VOC 0.05 09
Emission Control
HAP/TAP CAS Emissions Estimation Efficiency Emission
Pollutants (in HAP/TAPS EF Control
Alphabetical Order) (see instructions) (pounds/Year) Method Code (Net after all Factor
See Instructions controls)
2008
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 2008
1. Emission Source ID(from permit)or IES 17
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 2008: 51086 TON/yr
(e.g.production or fuel use):
6. Fuel Information (If fuel is used) /o Sulfur % Ash Heat Content
Btu/units
7. Capture Efficiency
(%of Emissions from this Process Vented to Control
Device or Stack): —
8. Control Device Information :None
Order CS—ID CD ID Control Device Description
as listed inpermit)
9. Emission Release Point RP Information: Sources vented to more than one ERP use additional ntry lines):
ERP ID ERP Type Height Diameter Temperature Velocity Volume Flow ERP Description
(in feet) Circle(enter#): (F) (Feet/sec) Rate(Acfm)
Rectangle(L x W)
in 0.1 feet)
EP-17 VERTICAL STACK 6 1 0.42 130---F 59.5 494.6 stack
55

Operating Scenario: OS — 33 Emission Source/Group ID: IES 17
10. Operating Schedule: (Source/Operating Scenario that best characterizes Calendar Year 2008)
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/ March—May 25% June—Aug. 25% Sept.—Nov. 25%
2008 2008 2008 2008
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
2008
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)
2008
CO CO 08
NOx NOx 08
TSP TSP 6.9 08 0.27
PM10 PM10 6.9 08 0.27
PM2.5 PM2.5 08
S02 S02 08
VOC VOC 08
HAP/TAP Emissions Emission Control
Pollutants (in CAS HAP/TAPS Estimation Efficiency Emission EF Control
(see instructions) Method Code Factor
Alphabetical Order) (Pounds/Year) (Net after all controls)
See Instructions
2008
56

Facility Total CY 2008 Emissions Summary
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 2008
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 2008 2007 %Difference
Carbon Dioxide CO2 124389 46777.45 Not reported N/A
Methane CH4 74-82-8 1.1227 Not reported N/A
Nitrous Oxide 20 10024972 0.6149 Not reported N/A
Criteria Pollutants
Actual Emissions Tons/Year
Pollutant CAS 2008 2007 %Difference
CO CO 26.2 12.59 108.10167%
NOx NOx 66.29 125.01 —46.97224%
PM TSP TSP 27.82 42.31 —34.247223%
PM10 PM10 25.0 36.71 —31.898663%
PM2.5 PM2.5 7.35 15.55 —52.733124%
S02 S02 166.31 336.95 —50.642532%
VOC VOC 12.7 34.51 —63.19907%
Hazardous Air Pollutants HAPS and/or Toxic Air Pollutants TAPS
Actual Emissions Pounds/Year
Pollutant I CAS 1 2008 2007 %Difference
Pollutant Grou :Antimon Com ounds total mass inc elemental SB Grou Sum:5.56756
Antimony Unlisted Compounds SBC—Other 5.56756 14.31806 —61.115124%
(Specify Component of SBC
Pollutant Group:Arsenic Compounds(total mass of elemental AS,arsine and all inorganic compounds) Group
Sum:1.39966
Arsenic Unlisted Compounds( ASC—Other 1.39966 3.5979 —61.09786%
Specify Component of ASC
Pollutant Group:Beryllium compounds Total mass Gr up Sum:.02948
Beryllium Compound,Unlisted BEC—Other 0.02948 .0758 —61.108185%
(Specify Com onent of BEC
Pollutant Grou :Cadmium compounds total mass inc elemental metal Group Sum:.42204
Cadmium Unlisted Compounds CDC—Other 0.42204 1.08514 —61.107323%
(Specify Com onent of CDC
57

Pollutant Grou :Cobalt com ounds Group Sum:6.383
Cobalt Unlisted Compound COC-Other 6.383 16.4053 -61.091846%
(Specify Component of COC
Pollutant Grou :Lead and Lead compounds Group Sum:1.60128
Lead Unlisted Compounds PBC-Other 1.60128 4.11742 -61.10963%
(Specify and Component of PBC
ollutant Grou :Man anese compounds Group Sum:3.18106
Manganese Unlisted Compounds MNC-Other 3.18106 8.17704 -61.09766%
(Specify Component of MNC
Pollutant Group:Mercury Compounds-all total mass, in Hg Vapor Group Sum:.13486
Mercury Unlisted Compounds HGC-Other 0.13486 .47568 -71.64901%
(Specify Component of HGC 7
Pollutant Grou :Nickel Com ounds, sum total mass inc elemental Group Sum:89.60694
Nickel Unlisted Compounds NIC-Other 89.60694 230.4025 -61.108524%
(Specify Component of NIC
Pollutant Grou :Chromium(VI) on-Specific Com ounds as Chrom VI (Com onent CRC Group Sum:.75848
Chromium(VI)Non-Specific,
Unlisted(Specify Component of NSCR6-Other 0.75848 .77078 -1.5957879%
NSCR6 CRC
Pollutant Grou :Chromium-Al Total Inc Chromium categories,metal and Others Group Sum:.89608
Chromium(VI)Non-Specific,
Unlisted(Specify Component of NSCR6-Other 0.75848 .77078 -1.5957879%
NSCR6 CRC
Chromium Unlisted Compounds CRC-Other 0.1376 1.53324 -91.02554%
(Specify Component of CRC
Pollutant Grou :Pol c clic Or anic Matter(Specific Co m ounds from OA PS for TV Group Sum:1.92981
Benzo(a)pyrene(Component of 50-32-8 0.00115 .00128 -10.156246%
POMTV POM7
Naphthalene(Component of 91-20-3 1.92866 5.41668 -64.39406%
POMTV
Pollutant Grou :Pol c clic Or anic Matter 7 PAH Com ounds for NIF Grou Sum:.00115
Benzo(a)pyrene(Component of 50-32-8 0.00115 .00128 -10.156246%
POMTV POM7
Acetaldehyde 75-07-0 0.112 .127 -11.811024%
Acrolein 107-02-8 0.188 .038 394.73682%
Ammonia as NH3 7664-41-7 15440.0 13080 18.042814%
Benzene 71-43-2 3.7554 4.80082 -21.775862%
Ethyl benzene 100-41-4 0.0759 .26772 -71.64948%
Fluorides(sum of all fluoride 16984-48-8 44.51792 157.01278 -71.64694%
com ounds
Formaldehyde 50-00-0 51.07418 179.30196 -71.51499%
Methyl chloroform 71-55-6 0.28168 .99344 1 -71.645996%
Phosphorus Metal,Yellow or 7723-14-0 10.03002 25.77504 -61.086308%
. White
Polycyclic Organic Matter(Inc
PAH,dioxins,etc.NC AP 42 POM 2.21242 4.35082 -49.149357%
historic amorphous lob
Selenium Compounds SEC 0.72432 1.8628 -61.116592%
Toluene 108-88-3 8.64976 27.51864 -68.567635%
X lene,o- 95-47-6 0.9901 1.42882 -30.705055%
58

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
Comments From Facility:
59

Emissions by Operating Scenario for Pollutant
2008 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
6 jenerator for Emergency Power/Peak Shaving 170 S-22B
o. 6 fuel—oil fired boilers(20.3 million Btu per 848 3 S-5
our heat input)
3 atural gas/saleable animal fat/no.6 oil fired boiler 1928.01 S-8
84 million Btu per hour heat input)
5 jenerator for Emergency Power/Peak Shaving 190 S-22A
2 atural gas/saleable animal fat/no.6 oil fired boiler 15105.18 S-8
84 million Btu per hour heat input)
4 atural gas/saleable animal fat/no.6 oil fired boiler 1928.01 S-9
[atural
million Btu hour heat input)
5 gas/saleable animal fat/no.6 oil fired boiler 15105.18 S-9
million Btu hour heat in ut7 ane—fired Sin ers for sin ein ul 54.47 —ES-7
6 fuel—oil fired boilers(20.3 million Btu per 848 3 S-4
heat input)
Methane CH4
+804�ml
fuel—oil fired boilers(20.3 million Btu per 22 S-4
eat input)
7e—fired Singers for singeing poultry01 —ES-7
4 gas/saleable animal fat/no.6 oil fired boiler07 S-9
illion Btu per hour heat input)
5 atural gas/saleable animal fat/no.6 oil fired boiler.256 S-9
84 million Btu per hour heat input)
5 jenerator for Emergency Power/Peak Shaving 011 S-22A
2 atural gas/saleable animal fat/no.6 oil fired boiler 256 S-8
jenterator
illion Btu hour heat input)
6 fuel—oil fired boilers(20.3 million Btu per 22 S-5
heat input)
3ral gas/saleable animal fat/no.6 oil fired boiler 07 S-8
million Btu per hour heat input)
6 for Emergency Power/Peak Shaving 0097 S-22B
Nitrous Oxide 20
3484
ral gas/saleable animal fat/no.6 oil fired boiler 01 S-8
million Btu r hour heat in ut5erator for Emer en Power/Peak Shavin 0015 S-22A
6 fuel—oil fired boilers(20.3 million Btu per 02 S-4
heat input)
1

atural gas/saleable animal fat/no.6 oil fired boiler.
4 84 million Btu r hour heat input) 01 S-9
atural gas/saleable animal fat/no.6 oil fired boiler.
5 84 million Btu hour heat input)
256 S-9
atural gas/saleable animal fat/no.6 oil fired boiler
2 84 million Btu hour heat input) 256 S-8
Lenerator
6 fuel—oil fired boilers(20.3 million Btu per 02 S-5
heat input)
6 for Emer en Power/Peak Shavin 0014 S-22B
7 ane—fired Singers for singeing poultry 04 —ES-7
CO
0 ookers IOA and IOB S—I0BES-10A.1
18 )oultry meal storage silo S-15
4 tural gas/saleable animal fat/no.6 oil fired boiler.37 S-9
84 million Btu per hour heat input)
9 ultry meal storage silo S-13
3 oultry meal conveyance system IES17
6 enerator for Emergency Power/Peak Shaving 84 S-22B
19 ive poultry receiving and handling system S-1
1 ive poultry receiving and handling system S-3
2 atural gas/saleable animal fat/no.6 oil fired boiler 10.54 S-8
84 million Btu per hour heat input)
atural gas/saleable animal fat/no.6 oil fired boiler
5 84 million Btu hour heat input) 10.54 S-9
o.6 fuel—oil fired boilers(20.3 million Btu per 1.12 S-4
our heat input)
3 atural gas/saleable animal fat/no.6 oil fired boiler.37 S-8
84 million Btu per hour heat input)
1 rocess room air collection S-1 OD
5 enerator for Emergency Power/Peak Shaving 91 S-22A
4 ultry meal loadout area(54 tons per hour 5-19
a city)
6 efri eration system —ES-6
7 ro ane—fired Singers for singeing poultry 39 —ES-7
17 3oultry meal storage silo S-14
2 Multry meal storage silo 5-16
0 live poultry receiving and handling system S-2
15 poultry meal storage silo 5-12
o.6 fuel—oil fired boilers(20.3 million Btu per 1.12 S-5
our heat input)
11 1poultry meal storage silo S-11
NOx
0 ookers IOA and IOB S—I0BES-10A.1
o.6 fuel—oil fired boilers(20.3 million Btu per
12.34
our heat input) S-4
F6 enerator for Emergency Power/Peak Shaving .7 S-22B
18 ul meal storage silo S-15
9 oultry meal storage silo S-13
2

3 oultry meal conveyance system IES17
5 enerator for Emergency Power/Peak Shaving S-22A
19 ive poultryreceivingand handlingsystem S-1
1 ive poultry receiving and handling system S-3
7 ro ane—fired Singers for singeing poultry 67 —ES-7
atural gas/saleable animal fat/no.6 oil fired boiler
2 84 million Btu hour heat input) 12.55 S-8
1 3rocess room air collection S-1 OD
4 oultry meal loadout area(54 tons per hour S-19
a aci
3iatural gas/saleable animal fat/no.6 oil fired boiler 4.07 S-8
84 million Btu per hour heat input)
atural gas/saleable animal fat/no.6 oil fired boiler
5 84 million Btu hour heat input) 12.55 S-9
6 _refrigeration system —ES-6
o.6 fuel—oil fired boilers(20.3 million Btu per 12.34 S-5
our heat input)
17 3oultry meal storage silo S-14
4 atural gas/saleable animal fat/no.6 oil fired boiler 4.07 S-9
84 million Btu per hour heat input)
2 3oultry meal storage silo S-16
0 Vive oul receivin and handl' s stem S-2
11 l meal story a silo S-11
15 l meal storage silo S-12
PM TSP
0 kookers IOA and IOB S—I0BES-10A.1
17 ul meal storage silo S-14
18 oul meal storage silo S-15
5 enerator for Emergency Power/Peak Shaving12 S-22A
19 ive poultryreceivingand handlingsystem S-1
6 enerator for Emergency Power/Peak Shaving11 S-22B
atural gas/saleable animal fat/no.6 oil fired boiler
4 84 million Btu r hour heat input) 87 S-9
9 oul meal storage silo S-13
1 rocess room air collection S—I OD
15 oul meal storage silo S-12
6 efri eration system —ES-6
4 oultry meal loadout area(54 tons per hour 5.23 S-19
a aci
11 oul meal storage silo S-11
0 ive poultryreceivingand handlingsystem S-2
1 ive poultryreceivingand handlingsystem S-3
atural gas/saleable animal fat/no.6 oil fired boiler
5 84 million Btu r hour heat input) 95 S-9
7 ro ane—fired Singers for singeing poultry04 —ES-7
3 oul meal conveyance stem .9 S 17
o.6 fuel—oil fired boilers(20.3 million Btu per 5.39 S-5
our heat input)
3 87 S-8
3

atural gas/saleable animal fat/no.6 oil fired boiler
84 million Btu per hour heat input)
2 ultry meal storage silo 0 ES-16
o.6 fuel-oil fired boilers(20.3 million Btu per .39 S-4
our heat input)
2 atural gas/saleable animal fat/no.6 oil fired boiler 95 S-8
84 million Btu per hour heat input)
PM 10
0 rou'll"try
ers l0A and IOB S-10BES-10A.1
fuel-oil fired boilers(20.3 million Btu per 4.38 S-5
heat input)
17 meal storage silo S-14
18 meal storage silo 0 ES-15
atural gas/saleable animal fat/no.6 oil fired boiler.
5 84 million Btu hour heat input) 72 S-9
5 enerator for Emergency Power/Peak Shaving 12 S-22A
19 ive poultry receiving and handling system S-1
6 enerator for Emergency Power/Peak Shaving 11 S-22B
9 Itry meal storage silo S-13
1 rocess room air collection S-lOD
15 Itry meal storage silo S-12
6 efri eration system -ES-6
4 oultry meal loadout area(54 tons per hour 5.23 S-19
a city)
11 Itry meal storage silo S-11
0 ive poultry receiving and handling system S-2
1 ive noultry receivin and handlin s stem S-3
7 roPane-fired Singers for singeing ul 04 -ES-7
3 oultry meal conveyance system 6.9 IES17
o.6 fuel-oil fired boilers(20.3 million Btu per 4.38 S-4
our heat input)
2 atural gas/saleable animal fat/no.6 oil fired boiler 72 S-8
84 million Btu per hour heat input)
L84
ral gas/saleable animal fat/no.6 oil fired boiler
3 million Btu r hour heat input) 7 S-8
4 ral gas/saleable animal fat/no.6 oil fired boiler 7 S-9
million Btu r hour heat in ut2 l meal storage silo S-16
PM2.5
0 ookers l0A and IOB S-10BES-10A.1
18 ul meal storage silo S-15
9 oul meal storage silo S-13
3 ul meal conveyance system S 17
19 ive poultryreceivingand handlingsystem S-1
1 ive poultryreceivingand handlingsystem S-3
5 atural gas/saleable animal fat/no.6 oil fired boiler 24 S-9
84 million Btu r hour heat input)
5 enerator for Emergency Power/Peak Shaving12 S-22A
4

o. 6 fuel-oil fired boilers(20.3 million Btu per 85 S-5
our heat input)
tural gas/saleable animal fat/no.6 oil fired boiler
3 84 million Btu r hour heat input) 45 S-8
o.6 fuel-oil fired boilers(20.3 million Btu per 2.85 S-4
4 rour heat input)
6 enerator for Emergency Power/Peak Shaving 11 S-22B
1 rocess room air collection S-I OD
4 oultry meal loadout area(54 tons per hour 5-19
a ci
6 efri eration system -ES-6
17 ultry meal storage silo S-14
7 ro ane-fired Singers for singeing poultry 04 -ES-7
2 oultry meal storage silo 5-16
0 ive poultry receiving and handling system S-2
4 atural gas/saleable animal fat/no.6 oil fired boiler 45 ES-9
84 million Btu per hour heat input)
11 oultry meal storage silo S-11
15 ultry meal storage silo 5-12
atural gas/saleable animal fat/no.6 oil fired boiler
2 84 million Btu hour heat input)
24 S-8
SO2
0 ookers IOA and IOB S-I0BES-10A.1
o.6 fuel-oil fired boilers(20.3 million Btu per 3.98 S-5
our heat input)
18 oul meal storage silo S-15
9 our
meal storage silo S-13
3 +84tumral
meal conveyance stem ES17
19poultry receivingand handlingsystem S-1
1poultryreceivingand handlingstem S-3
gas/saleable animal fat/no.6 oil fired boiler3illion Btu r hour heat input) 03 S-8
7 ro ane-fired Singers for singeing ul -ES-7
2 atural gas/saleable animal fat/no.6 oil fired boiler 08 S-8
84 million Btu per hour heat input)
1 3rocess room air collection S-1 OD
4 r84tmillion
meal loadout area(54 tons per hour S-19
5 or for Emergency Power/Peak Shaving07 S-22A
el-oil fired boilers(20.3 million Btu per 3.98 S-4
t input)
as/saleable animal fat/no.6 oil fired boiler
5 Btu r hour heat input)
08 S-9
6 -effiggeration system -ES-6
17 vultry meal storage silo S-14
4 tural gas/saleable animal fat/no.6 oil fired boiler 9.03 S-9
84 million Btu r hour heat input)
2 Wultry meal storage silo 5-16
6 lGenerator for Emergency Power/Peak Shaving 06 S-22B
5

0 Live oul receivin and handlin s stem S-2
l meal stora a silo S-11
15 l meal storage silo S-12
VOC
1 rocess room air collection 1 S-1 OD
o.6 fuel—oil fired boilers(20.3 million Btu per 06 S-4
our heat input)
18 oul meal storage silo S-15
7 ro ane—fired Singers for singeing poultry05 —ES-7
9 oul meal storage silo S-13
3 oul meal conveyance system S 17
o.6 fuel—oil fired boilers(20.3 million Btu per 06 S-5
our
heat input)
19 ive poultryreceivingand handlingsystem S-1
1 ive poultryreceivingand handlingstem S-3
atural gas/saleable animal fat/no.6 oil fired boiler
4 84 million Btu hour heat input) 02 S-9
5 L84million
ator for Emergency Power/Peak Shaving12 S-22A
5 l gas/saleable animal fat/no.6 oil fired boiler 69 S-9
Btu r hour heat in ut6 ator for Emergency Power/Peak Shaving 11 S-22B
4 ultry meal loadout area(54 tons per hour S-19
a aci
6 efri eration system —ES-6
17 :)oultry meal storage silo S-14
2 atural gas/saleable animal fat/no.6 oil fired boiler 69 S-8
84 million Btu r hour heat input)
0 okers l0A and IOB 10.78 S-10BES-10A.1
2 oultry meal storage silo S-16
0 ive poultry receiving and handling system S-2
3 tural gas/saleable animal fat/no.6 oil fired boiler.02 S-8
84 million Btu per hour heat input)
11 ultry meal storage silo S-11
15 ultry meal storage silo S-12
Process ID Operating Scenario Emission Rate(Pounds/Yr)Emission Source ID
Acetaldeh de
6 enerator for Emergency Power/Peak Shaving 054 S-22B
5 lGenerator for Emergency Power/Peak Shaving 058 S-22A
Acrolein
5 lGenerator for Emergency Power/Peak Shavin 018 S-22A
6 IGenerator for Emergency Power/Peak Shaving 17 S-22B
Ammonia as NH3
6 keffigeration system 115440 —ES-6
Antimony Unlisted Compounds(Specify Component of SBC)
6

3 atural gas/saleable animal fat/no.6 oil fired boiler 42759 S-8
84 million Btu per hour heat input)
4 atural gas/saleable animal fat/no.6 oil fired boiler.42759 S-9
84 million Btu per hour heat input)
o.6 fuel—oil fired boilers(20.3 million Btu per .35619 S-4
our heat input)
o. 6 fuel—oil fired boilers(20.3 million Btu per .35619 S-5
our heat input)
Arsenic Unlisted Compounds Specify Component of ASC
o.6 fuel—oil fired boilers(20.3 million Btu per 59241 S-5
our heat input
3 total gas/saleable animal fat/no.6 oil fired boiler 10742 S-8
84 million Btu per hour heat input)
4 tural gas/saleable animal fat/no.6 oil fired boiler 10742 S-9
84 million Btu per hour heat input)
o. 6 fuel—oil fired boilers(20.3 million Btu per 59241 S-4
our heat input)
Benzene
atural gas/saleable animal fat/no.6 oil fired boiler
3 84 million Btu per hour heat input) 03166 S-8
5 enerator for Emergency Power/Peak Shaving 1.8 S-22A
o.6 fuel—oil fired boilers(20.3 million Btu per 09604 S-5
our heat input)
6 jenerator for Emergency Power/Peak Shaving 1.7 S-22B
o.6 fuel—oil fired boilers(20.3 million Btu per 09604 S-4
our heat input)
4 atural gas/saleable animal fat/no.6 oil fired boiler 03166 S-9
84 million Btu r hour heat input)
Benno a ene(Component of POMTV POM7
5 enerator for Emer enc Power/Peak Shaving0006 S-22A
6 lGenerator for Emergency Power/Peak Shaving 00055 S-22B
Berylliurn Compound,Unlisted(Specify Component of BEC
o.6 fuel—oil fired boilers(20.3 million Btu per 01248 S-4
our heat input)
3 atural gas/saleable animal fat/no.6 oil fired boiler.00226 S-8
84 million Btu per hour heat input)
o.6 fuel—oil fired boilers(20.3 million Btu per 01248 S-5
our heat input)
4 total gas/saleable animal fat/no.6 oil fired boiler 00226 S-9
84 million Btu per hour heat input)
Cadmium Unlisted Compounds(Specify Com onent of CDC
3 atural gas/saleable animal fat/no.6 oil fired boiler 0324 S-8
84 million Btu r hour heat input)
o.6 fuel—oil fired boilers(20.3 million Btu per 17862 S-5
our heat input)
o.6 fuel—oil fired boilers(20.3 million Btu per 17862 S-4
our heat input)
7

atural gas/saleable animal fat/no.6 oil fired boiler
4 84 million Btu r hour heat" ut 10324 FS-9
Chromium Non—Specific,Unlisted(Specify Component of NSCR6 CRC
o.6 fuel—oil fired boilers(20.3 million Btu per 37924 S-4
our heat input)
o.6 fuel—oil fired boilers(20.3 million Btu per 37924 S-5
our heat input)
Chromium Unlisted Compounds(Specify Component of CRC
atural gas/saleable animal fat/no.6 oil fired boiler
3 84 million Btu hour heat input) 0688 S-8
atural gas/saleable animal fat/no.6 oil fired boiler
4 84 million Btu r hour heat input) 0688 S-9
Cobalt Unlisted Compound(Specify Component of COO
[84
ral gas/saleable animal fat/no.6 oil fired boiler
3 million Btu r hour heat input) 48973 S-8
6 fuel—oil fired boilers(20.3 million Btu per 2.70177 S-5
heat input)
6 fuel—oil fired boilers(20.3 million Btu per .70177 S-4
heat input)
ral gas/saleable animal fat/no.6 oil fired boiler
4 million Btu r hour heat in ut 48973 S-9
Eth lbenzene
o.6 fuel—oil fired boilers(20.3 million Btu per 02854 S-5
our heat input)
4 atural gas/saleable animal fat/no.6 oil fired boiler 00941 S-9
84 million Btu per hour heat input)
Ef84
1 gas/saleable animal fat/no.6 oil fired boiler 00941 S-8
illion Btu r hour heat i utfuel—oil fired boilers(20.3 million Btu per 02854 S-4
eat input)
Fluorides sum of all fluoride compounds)
o.6 fuel—oil fired boilers(20.3 million Btu per 16.7402 S-4
our heat input)
atural gas/saleable animal fat/no.6 oil fired boiler
3 84 million Btu r hour heat input) 51876 S-8
o.6 fuel—oil fired boilers(20.3 million Btu per 16.7402 S-5
our heat input)
4 atural gas/saleable animal fat/no.6 oil fired boiler 51876 S-9
184 million Btu per hour heat input)
Formaldeh de
5 jenerator for Emergency Power/Peak Shaving 18 S-22A
o.6 fuel—oil fired boilers(20.3 million Btu per 19.07396 S-4
our heat input)
3 atural gas/saleable animal fat/no.6 oil fired boiler 6.28813 S-8
84 million Btu per hour heat input)
19.07396 S-5
8

o. 6 fuel—oil fired boilers(20.3 million Btu per
our heat input)
atural gas/saleable animal fat/no.6 oil fired boiler
4 84 million Btu r hour heat input) •28813 S-9
6 enerator for Emergency Power/Peak Shaving 17 S-22B
Lead Unlisted Compounds(Specify and Component of PBC
No. 6 fuel—oil fired boilers(20.3 million Btu per 67769 S-4
our heat input)
No.6 fuel—oil fired boilers(20.3 million Btu per
our heat input) 67769 S-5
atural gas/saleable animal fat/no.6 oil fired boiler
3 84 million Btu r hour heat input)
12295 S-8
4 atural gas/saleable animal fat/no.6 oil fired boiler 12295 S-9
84 million Btu r hour heat input)
Manaanese Unlisted Compounds(Specify Component of MNC
No.6 fuel—oil fired boilers(20.3 million Btu per
our heat input)
1.3464 S-5
No.6 fuel—oil fired boilers(20.3 million Btu per 1.3464 S-4
our heat input)
3 atural gas/saleable animal fat/no.6 oil fired boiler 24413 S-8
84 million Btu per hour heat input)
atural gas/saleable animal fat/no.6 oil fired boiler
4 84 million Btu r hour heat input) 24413 S-9
Merc Unlisted Com unds(Specify Component of HGC
o.6 fuel—oil fired boilers(20.3 million Btu per 05071 S-5
our heat input
3 atural gas/saleable animal fat/no.6 oil fired boiler 01672 S-8
84 million Btu per hour heat input)
o.6 fuel—oil fired boilers(20.3 million Btu per 05071 S-4
our heat input
4 atural gas/saleable animal fat/no.6 oil fired boiler 01672 S-9
84 million Btu per hour heat input)
Meth 1 chloroform
3 r84million
l gas/saleable animal fat/no.6 oil fired boiler 03492 S-8
llion Btu hour heat input)
fuel—oil fired boilers(20.3 million Btu per 10592 S-5
eat input)
fuel—oil fired boilers(20.3 million Btu per 10592 S-4
eat input)
4 l gas/saleable animal fat/no.6 oil fired boiler 03492 S-9
Btu per hour heat input)
Na hthalene(Component of POM
4 atural gas/saleable animal fat/no.6 oil fired boiler 16719 S-9
84 million Btu hour heat input)
5 enerator for Emergency Power/Peak Shaving 3 S-22A
6 enerator for Emergency Power/Peak Shaving 28 S-22B
3 16719 S-8
9

atural gas/saleable animal fat/no.6 oil fired boiler
84 million Btu per hour heat input)
No.6 fuel—oil fired boilers(20.3 million Btu per 50714 S-4
our heat input)
No.6 fuel—oil fired boilers(20.3 million Btu per 50714 S-5
our heat input)
Nickel Unlisted Com unds(Svecify Component of NIC
o.6 fuel—oil fired boilers(20.3 million Btu per 37.92352 S-5
our heat input)
o. 6 fuel—oil fired boilers(20.3 million Btu per 37.92352 S-4
our heat input)
3 atural gas/saleable animal fat/no.6 oil fired boiler 6.87995 S-8
84 million Btu hour heat input)
4 atural gas/saleable animal fat/no.6 oil fired boiler 6.87995 S-9
i84 million Btu per hour heat input)
Phosphorus Metal Yellow or White
4 atural gas/saleable animal fat/no.6 oil fired boiler 76937 S-9
lo.
4 million Btu r hour heat input)
3 atural gas/saleable animal fat/no.6 oil fired boiler 76937 S-8
4 million Btu r hour heat input)
6 fuel—oil fired boilers(20.3 million Btu per .24564 S-5
our heat input)
No. 6 fuel—oil fired boilers(20.3 million Btu per .24564 S-4
our heat input)
PoIveyclic Orizanic Matter Inc PAH dioxins etc.NC AP 42 historic amorphous lob
5 JGenerator for Emergency Power/Peak Shaving 49 S-22A
6 enerator for Emergency Power/Peak Shaving 45 S-22B
o.6 fuel—oil fired boilers(20.3 million Btu per 53856 S-5
our heat input)
o.6 fuel—oil fired boilers(20.3 million Btu per 53856 S-4
our heat input)
L184l gas/saleable animal fat/no.6 oil fired boiler 09765 S-8
illion Btu hour heat in ut1 gas/saleable animal fat/no.6 oil fired boiler 09765 S-9
illion Btu hour heat i ut
Selenium Com ounds
3 atural gas/saleable animal fat/no.6 oil fired boiler 05563 S-8
84 million Btu per hour heat input)
4 [84million
l gas/saleable animal fat/no.6 oil fired boiler 05563 S-9
Btu r hour heat in utfuel—oil fired boilers(20.3 million Btu per 30653 S-5
eat in utfuel—oil fired boilers(20.3 million Btu per 30653 S-4
eat input)
Toluene
o.6 fuel—oil fired boilers(20.3 million Btu per
our heat input)
78255 S-4
10

o.6 fuel—oil fired boilers(20.3 million Btu per
our heat input) 78255 S-5
atural gas/saleable animal fat/no.6 oil fired boiler
3 84 million Btu input)
r hour heat91733 S-8
4 atural gas/saleable animal fat/no.6 oil fired boiler 91733 S-9
84 million Btu hour heat input)
6 enerator for Emergency Power/Peak Shaving 6 S-22B
5 enerator for Emergency Power/Peak Shaving 65 S-22A
X lene o-
4 atural gas/saleable animal fat/no.6 oil fired boiler 01613 S-9
I'atural
4 million Btu r hour heat input)
5 enerator for Emergency Power/Peak Shaving45 S-22A
3 gas/saleable animal fat/no.6 oil fired boiler 01613 4z-8
84 million Btu per hour heat input)
o. 6 fuel—oil fired boilers(20.3 million Btu per 04892 S-5
our heat input)
6 Fo.6 fuel—oil fired boilers(20.3 million Btu per 04892 S-4
our heat input)
enerator for Emergency Power/Peak Shaving 41 S-22B
11

Facility Total CY 2008 Emission Summary Facility Id : 0800081
Green House Gases Pollutants GHG
Actual Emissions Tons/Year
Pollutant CAS 2008 2007 % Difference
Carbon Dioxide CO2 124389 46777.45 Not reported N/A
Methane CH4 74-82-8 1.1227 Not reported N/A
Nitrous Oxide N20 10024972 0.6149 Not reported N/A
CO2 equivalent(sum of individual GHG pollutant emission
times their 1995 IPCC Global Warming Potential(GWP), 42,630.82 metric tons
converted to metric tons
Criteria Pollutants
Actual Emissions Tons/Year
Pollutant CAS 2008 2007 % Difference
CO CO 26.2 12.59 108.10167%
NOx NOx 66.29 125.01 -46,97224%
PM TSP TSP 27.82 42.31 -34.247223%
PM 10 PM 10 25.0 36.71 -31.898663%
PM2.5 PM2.5 7.35 15.55 -52.733124%
S02 S02 166.31 336.95 -50.642532%
VOC VOC 12.7 34.51 -63.19907%
Hazardous Air Pollutants(RAPS) and/or Toxic Air Pollutants(TAPs)
Actual Emissions Pounds/Year
Pollutant CAS 1 2008 1 2007 % Difference
Antimony&Compounds total mass, inc elemental SB 5.56756
Antimony Unlisted Compounds SBC-Other 5.56756 _T 14.31806 -61.115124%
(Specify&Component of SBC
rsenic& Compounds (total mass of elemental AS, arsine and all inorganic compounds)1.39966
Arsenic Unlisted Compounds I ASC-Other 1.39966 3.5979 _T -61,09786%
(Specify&Component of ASC
er Ilium &compounds Total mass .02948
Beryllium Compound, Unlisted BEC-Other 0.02948 .0758 -61.108185%
(Specify&Component of BEC
admium & compounds total mass inc elementai metal .42204
Cadmium Unlisted Compounds CDC-Other 0A2204 1.08514 -61.107323%
(Specify&Component of CDC
obalt com ounds6.383
It Unlisted Compound(Specify COC-Other 6.383 16.4053 _T 61.091846%
&Component of COC
ead and Lead compounds 1.60128
Lead Unlisted Compounds(Specify PBC-Other 1.60128 4.11742 -61.10963%
and Component of PBC
an anese&com ounds3.18106 __F
Manganese Unlisted Compounds MNC-Other 3.18106 8.17704 -61.09766%
(Specify&Component of MNC
ercury& Compounds- all total mass, inc Hg Vapor.13486
Mercury Unlisted Compounds HGC-Other 0.13486 .47568 -71.64901%
&Component of HGC
r
Com ounds sum total mass inc elemental89.60694
el Unlisted Compounds NIC-Other 89.60694 230.4025 -61.108524%
&Com Went of NICm VI Non-S ecific Com ounds as Chrom VI Com onent CRC .75848
mium (VI)Non-Specific,

Unlisted(Specify&Component of NSCR6-Other 0.75848 .77078 -1.5957879%
NSCR6&CRC
Chromium -All Total Inc Chromium VI categories, metal and Others .89608
Chromium (VI) Non-Specific,
Unlisted(Specify&Component of NSCR6-Other 0.75848 .77078 -1.5957879%
NSCR6&CRC
Chromium Unlisted Compounds CRC-Other 0.1376 1.53324 -91.02554%
(Specify&Component of CRC
of c clic Organic Matter(Specific Com ounds from OAQPS for TV 1.92981
Benzo(a)pyrene(Component of 50-32-8 0.00115 .00128 -10.156246%
POMTV& POM7
Naphthalene(Component of 91-20-3 1.92866 5,41668 -64.39406%
POMTV
of c ciic Organic Matter 7 PAH Com ounds for NIF .00115
Benzo(a)pyrene(Component of 50-32-8 0.00115 .00128 -10.156246%
POMTV& POM7
Acetaldehyde 75-07-0 0.112 .127 -11.811024%
Acrolein 107-02-8 0.188 .038 394.73682%
Ammonia as NH3 7664-41-7 15440.0 13080 18.042814%
Benzene 71-43-2 3.7554 4.80082 -21.775862%
Ethyl benzene 100-41-4 0.0759 .26772 -71.64948%
Fluorides(sum of all fluoride 16984-48-8 44.51792 157.01278 -71.64694%
compounds)
Formaldehyde 50-00-0 51.07418 179.30196 -71,51499%
Methyl chloroform 71-55-6 0.28168 .99344 -71.645996%
Phosphorus Metal, Yellow or White 7723-14-0 10.03002 25.77504 -61.086308%
Polycyclic Organic Matter(Inc PAH,
dioxins, etc. NC &AP 42 historic POM 2.21242 4.35082 -49.149357%
amorphous lob
Selenium Compounds SEC 0.72432 1.8628 -61.116592%
Toluene 108-88-3 8.64976 27,51864 -68.567635%
X lene, o- 95-47-6 0.9901 1.42882 -30.705055%

PERDUE FARMS,INC. - LEWISTON PROTEIN CONVERSION
Protein Conversion Emissions Inventory
ACTUAL CALCULATIONS FOR TSP
PROCESS DESCRIPTION In Tons Control* TSP Emission TSP Actual TSP ACT.
LEWISTON PROTEIN CONY. Efticienc Factor Ib/ton Emissions LB/HR
POULTRY MEAL SILO ES16 8,514 0.001 0.27 2.30 0.0003
POULTRY MEAL SILO / ISII 8,514 0.001 0.27 2.30 0.0003
POULTRY MEAL SILO 1 S 15 8,514 0.001 0.27 2.30 0.0003
POULTRY MEAL SILO 1 S 12 8,514 0.001 0.27 2.30 0.0003
v1c.�o-.e'� O R E O Y,cNC 7S1 5J,6$6 1 -15793.14 .0:
5 yS-f Sro POULTRY MEAL SILO FS14 8,514 0.001 0.27 2.30 0.0003
0 POULTRY MEAL SILO ✓ ES13 8,514 0.001 0.27 2.30 0.0003
POULTRY MEAL GRADING ES18 51,086 0.001 0.27 13.79 0.0020
POULTRY MEAL LOADOUT IF S 19 50,749SPIXVO 0.27 12332.12 1.7966
TSP 26153.05
l
ho4 J» ED � "toK 6/C, Zrrn55lan fs —04 5 Total in lbs/Yr
In Tons Year
13.077
*Efficiency Factors
a. Bagfilter contol(1,999)=.001%
rh,s is C.- �� C &;�-v'LQ - -74A CotAe
j/lie
� i7Y A
lyQ�r rniss��- �hls /h 1 n,ve"70`y

PERDUE FARMS,INC. - LEWISTON PROCESSING
ACTUAL CALCULATIONS FOR TSP
PROCESS DESCRIPTION ES Chickens Control* TSP Emission TSP Actual TSP Actual
LEWISTON PROCESSING # Processed Efficiency Factor(lb/BIRD) Emissions lb/hr LBM
RECEIVING LINE#1 ES 1 33,156,685 0.001 0.0003 9.95 0.0024
RECEIVING LINE#2 ES 2 33,156,685 0.001 0.0003 9.95 0.0024
RECEIVING LINE#3 ES 3 1 33,156,685 0.001 0.0003 9.95 0.0024
TSP 29.84
Total in lbs/Yr
In Tons Year
0.015
*Efficiency Factors
a.Bagfilter contol(1-.999)=.001%
*Emission Factors
a.Engineering estimate of I00lb/Itr per 100,000 chikens a day processed. Emission Factor based on this of.0003 lb/hr
per bird.
b.No%of TSP is known to be PM 10

/ 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 Watt-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): 126 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): 217,291 Annual Output kW-hr: 229,950
Annual Output h -hr: 331,128 <-----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 Ibl 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 NO NA
NO.,uncont. 6.3E+01 7.9E+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 ND NA
TOC(as CH4) 1.9E+00 2.3E+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 9.1E-01 5.50E-03 C CO 2.0E+01 2.5E+03 1.2E+00 7.50E-03 D
S% 1.1E+00 1.3E+02 6.7E-02 4.05E-04 B sox 5.5E-02 6.9E+00 3.5E-03 2.09E-05 B
Total HAP 3.1 E-02 4.0E+00 2.0E-03 1.19E-05
Lar est HAP I 1.4E-02 1.8E+00 9.0E-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 Ibl r
Acetaldehyde 4.6E-04 NA 5.8E-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 4.9E-01 1.48E-06 E,<
Toluene 5.2E-03 1.2E-01 6.5E-01 1.97E-06 E
X lenes 3.6E-03 8.5E-02 4.5E-01 1.35E-061 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 RatingPollutant Ib/hr Ib/ r t Ib/h -hr Rating
Carbon Dioxide(CO2) 3.7E+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. AA
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.
1

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-228 available. DENR is not responsible for errors or omissions
Diesel Fuel Sulfur Content(%): 0.05 Annual Operation(hours): 116 that may be contained herein.
NG Fuel Sulfur Content(gr/mm cu ft): 2,000
Engine Output(hp): 2628 Generator Output(kW): 1826
Annual Electrical Output(kW-hr): 200,046 lAnnual Output(kW-hr): 211,700
Annual Output h -hr: 304,848 <-----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 2.1 E+02 1.1E-01 7.00E-04 B PM NA NA NA ND NA
PM-10 1.8E+00 2.1 E+02 1.1E-01 7.00E-04 B PM-10 NA NA NA NO NA
PM-2.5 1.8E+00 2.1 E+02 1.1E-01 7.00E-04 B PM-2.5 NA NA NA ND NA
NO.,uncont. 6.3E+01 7.3E+03 3.7E+00 2.40E-02 B NO.,uncont. 4.7E+01 5.5E+03 2.7E+00 1.80E-02 D
NO,Cont. 3.4E+01 4.0E+03 2.0E+00 1.30E-02 B NO,cont. NA NA NA NO NA
TOC(as CH4) 1.9E+00 2.1 E+02 1.1 E-01 7.05E-04 C TOC(as CH4) 1.4E+01 1.6E+03 8.1 E-01 5.29E-03 D
NMTOC 1.7E+00 2.0E+02 9.8E-02 6.42E-04 E NMTOC 3.5E+00 4.0E+02 2.0E-01 1.32E-03 E
CO 1.4E+01 1.7E+03 8.4E-01 5.50E-03 C CO 2.0E+01 2.3E+03 1.1E+00 7.50E-03 D
S% 1.1E+00 1.2E+02 6.2E-02 4.05E-04 B sox 5.5E-02 6.4E+00 3.2E-03 2.09E-05 B
Total HAP 3.1E-02 3.6E+00 1.8E-03 1.19E-05
Lar est HAP I 1.4E-02 1.7E+00 8.3E-04 5.43E-06
Toxic/Hazardous Air Pollutants There are no Toxic/Hazardous Air Pollutant emission factors for dual-fuel engines.
Pollutant Ib/hr Ib/da Ib/ r
Acetaldehyde 4.6E-04 NA 5.4E-02 1.76E-07 E
Acrolein 1.4E-04 NA 1.7E-02 5.52E-08 E
Benzene 1.4E-02 NA 1.7E+00 5.43E-06 E
Benzo(a)pyrene 4.7E-06 NA 5.5E-04 1.80E-09 E,<
Formaldehyde 1.5E-03 NA 1.7E-01 5.52E-07 E
Napthalene 2.4E-03 NA 2.8E-01 9.10E-07 E
Total PAH 3.9E-03 NA 4.5E-01 1.48E-06 E,<
Toluene 5.2E-03 1.2E-01 6.0E-01 1.97E-06 E
X lenes 3.6E-03 8.5E-02 4.1E-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 Pollutant Ib/hr Ib/ r t Ib/h hr Rating
Carbon Dioxide(CO2) 3.4E+05 1.7E+02 0.31 NA Carbon Dioxide(COA 2.5E+05 1.3E+02 0.23 NA
Methane(CH4) 1.9E+01 9.7E-03 0.0001 NA Methane(CH4) 1.2E+03 5.8E-01 0.004 NA
Nitrous Oxide(N20) 2.8E+00 1.4E-03 0.00001 NA Nitrous Oxide(N20) 2.8E+00 1.4E-03 0.00001 NA II
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 toxicthazardous 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.

FUEL OIL COMBUSTION EMISSIONS CALCULATOR REVISION D 6/12/2008-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.
This spreadsheet is for your use only and should be used with caution.DENR does not guarantee the accuracy of the Information contained. This
WNWspreadsheet 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 S E
COMPANY: Perdue Farms Incorporated MAX HEAT INPUT: 20.30 MMBTU/HR
FACILITY ID NO.: 800081 FUEL HEAT VALUE: 150,000 BTU/GAL
PERMIT NUMBER: 03085T28 ACTUAL ANNUAL FUEL USAGE: 448,799 GAL/YR
FACILITY CITY: Lewiston MAXIMUM ANNUAL FUEL USAGE: 1,185,520 GAL/YR
FACILITY COUNTY: Bertie MAXIMUM SULFUR CONTENT 21
USER NAME: Wayne Black REQUESTED PERMIT LIMITATIONS
EMISSION SOURCE DESCRIPTION: No.6 oil-fired Boiler MAX FUEL USAGE 1,185,520 GAL/YR
EMISSION SOURCE ID NO.: ES74 MAX.SULFUR CONTENT 21 %
TYPE OF CONTROL DEVICES POLLUTANT CONTROL EFF.
NONE/OTHER PM 0
NONE/OTHER S02 0
NONE/OTHER NOx C
CRITERIA AIR POLLUTANT EMISSIONS INFORMATION
ACTUAL EMISSIONS POTENTIAL EMSSIONS EMISSION FACTOR
(AFTER CONTROLS I LIMITS) (BEFORE CONTROLS I LIMITS) (AFTER CONTROLS/LIMITS) Ib/1 O3 aI
AIR POLLUTANT EMITTED Whir tons/ r Ib/hr tons/ r Whir tons/ r uncontrolled controlled
TOTAL PARTICULATE MATTER PM FPM+CPM 3.25 5.39 3.25 14.24 3.25 14.24 2.40E+01 2.40E+01
FILTERABLE PM(FPM) 3.05 5.05 3.05 13.35 3.05 13.35 2.25E+01 2.25E+01
CONDENSABLE PM(CPM) 0.20 0.34 0.20 0.89 0.20 0.89 1.50E+00 1.50E+00
FILTERABLE PM<10 MICRONS(PMro) 2.64 4.38 2.64 11.57 2.64 11.57 1 1.95E+01 1.95E+01
FILTERABLE PM<2.5 MICRONS(PM2,5) 1.72 2.85 1.72 7.54 1.72 7.54 1.27E+01 1.27E+01
SULFUR DIOXIDE(S02) 44.62 73.98 44.62 195.43 44.62 195.43 3.30E+02 3.30E+02
NITROGEN OXIDES(NO.) 7.44 12.34 7.44 32.60 7.44 32.60 5.50E+01 5.50E+01
CARBON MONOXIDE CO 0.68 1.12 0.68 2.96 0.68 2.96 5.00E+00 5.00E+00
VOLATILE ORGANIC COMPOUNDS VOC 0.04 0.06 0.04 0.17 0.04 0.17 2.80E-01 2.80E-01
LEAD 000 000 0.00 000 000 0.00 1.51E-03 1 51 E-03
GREENHOUSE GAS EMISSIONS INFORMATION
CARBON DIOXIDE(CO2) 3527.06 5848.30 1 3527,06 1 1544&511 352T06 2.61E+04 2.61E+04
METHANE(CH,) 0.13 0.22 0.13 0.59 0.13 0.59 9.90E-01 9.90E-01
NITROUS OXIDE(N20) 0.01 002 0.01 0.06 0,01 0.06 1 00E-01 1.00E-01
TOXIC/HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION
ACTUAL EMISSIONS POTENTIAL EMSSIONS EMISSION FACTOR
CAS (AFTER CONTROLS/LIMITS) (BEFORE CONTROLS I LIMITS) (AFTER CONTROLS I LIMITS( IV 03 al
TOXIC I HAZARDOUS AIR POLLUTANT NUMBER Ib/hr lbtyr Ib/hr lbtyr Whir Ib r uncontrolled controlled
Antimony&compounds (H) SBC 7.1E-04 2.4E+00 7.1E-04 6.2E+00 7.1E-04 6.2E+00 5.25E-03 5.25E-03
Arsenic&compounds (TH) ASC 1.8E-04 5.9E-01 1.8E-04 1.6E+00 1.8E-04 1.6E+00 1.32E-03 1.32E-03
Benzene (TH) 71432 2.9E-05 9.6E-02 2.9E-05 2.5E-01 2.9E-05 2.5E-01 214E-04 2.14E-04
Beryllium&compounds H) BEC 3.8E-06 1.2E-02 3.8E-06 3.3E-02 3.8E-06 3.3E-02 2.78E-05 2.78E-05
Cadium&compounds (TH) CDC 5.4E-05 1.8E-01 5.4E-05 4.7E-01 5.4E-05 4.7E-01 3.98E-04 3.98E-04
Chromium-All/Total H CRC 1.1 E-04 3.8E-01 1.1 E-04 1.0E+00 1.1 E-04 1.0E+00 8.45E-04 8.45E-04
Cobalt compounds H COC 8.1 E-04 2.7E+00 8.1 E-04 7.1 E+00 8.1 E-04 7.1 E+00 6.02E-03 6.02E-03
Eth(benzene H 100414 8.6E-06 2.9E-02 8.6E-06 7.5E-02 8.6E-06 7.5E-02 6.36E-05 6.36E-05
Fluondes sum fluoride compounds) T 16984488 5.0E-03 1.7E+01 5.0E-03 4.4E+01 5.0E-03 4.4E+01 3.73E-02 3.73E-02
Formaldehyde TH 50000 5.8E-03 1.9E+01 5.8E-03 5.0E+01 5.8E-03 5.0E+01 4.25E-02 4.25E-02
Lead and Lead compounds (H) PBC 2.0E-04 6.8E-01 2.0E-04 1.8E+00 2.0E-04 1.8E+00 1.51 E-03 1.51E-03
Manganese&compounds (TH) MNC 4.1 E-04 1.3E+00 4.1 E-04 3.6E+00 4.1 E-04 3.6E+00 3.00E-03 3.00E-03
Mercury&compounds (TH) HGC 1.5E-05 5.1 E-02 1.5E-05 1.3E-01 1.5E-05 1.3E-01 1.13E-04 1.13E-04
Methyl chloroform (TH) 71566 3.2E-05 1.1 E-01 3.2E-05 2.8E-01 3.2E-05 2.8E-01 2.36E-04 2.36E-04
Na thalene (H) 91203 1.5E-04 5.1 E-01 1.5E-04 1.3E+00 1.5E-04 1.3E+00 1.13E-03 1.13E-03
Nickle&compounds H) NIC 1.1 E-02 3.8E+01 1.1 E-02 1.0E+02 1.1 E-02 1.0E+02 8.45E-02 8.45E-02
Phosphorus Metal,Yellow or White (H) 7723140 1.3E-03 4.2E+00 1.3E-03 1.1E+01 1.3E-03 1.1E+01 9.46E-03 9.46E-03
POM rates uncontrolled H POM 1.6E-04 5.4E-01 1.6E-04 1.4E+00 1.6E-04 1.4E+00 1.20E-03 1.20E-03
Selenium compounds H SEC 9.2E-05 3.1 E-01 9.2E-05 8.1 E-01 9.2E-05 8.1 E-01 6.83E-04 6.83E-04
Toluene (TH) 108883 8.4E-04 2.8E+00 8.4E-04 7.4E+00 8.4E-04 7.4E+00 6.20E-03 6.20E-03
X lene TH 1330207 1.5E-05 4.9E-02 1.5E-05 1.3E-01 1.5E-05 1.3E-01 1.09E-04 1.09E-04
Total HAP 2.2E-02 7.4E+01 22E-02 2.0E+02 22E-02 2.0E+02 1.6E-01 1.6E-01
Lar et HAP HH) 1.14E-02 3.79E+01 1.14E-02 1.00E+02 1.14E-02 1.00E+02 8.45E-02 8.45E-02
TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR PERMITTING PURPOSES
EXPECTED ACTUAL EMISSIONS AFTER CONTROLS I LIMITATIONS EMISSION FACTOR
Ib/10' al
TOXIC AIR POLLUTANT CAS Num. Ib/hr lb/day Ib r uncontrolled Icontrolled
Arsenic&compounds TH ASC 1.79E-04 4.29E-03 1.56E+00 1.32E-03 1.32E-03
Benzene (TH) 71432 2.90E-05 6.95E-04 2.54E-01 2.14E-04 2.14E-04
Cadium&compounds (TH) CDC 5.39E-05 1.29E-03 4.72E-01 3.98E-04 3.98E-04
Fluorides(sum fluoride Compounds) (T) 169&4488 5.05E-03 1.21E-01 4.42E+01 3.73E-02 3.73E-02
Formaldehyde TH 50000 5.75E-03 1.38E-01 5.04E+01 4.25E-02 4.25E-02
Manganese&compounds TH MNC 4.06E-04 9.74E-03 3.56E+00 3.00E-03 3.00E-03
Mercury&compounds TH HGC I 1.53E-05 3.67E-04 1.34E-01 1.13E-04 1.13E-04
Methyl chloroform (TH) 71566 3.19E-05 7.67E-04 2.80E-01 I 2.36E-04 2.36E-04
Toluene TH 108883 8.39E-04 2.01E-02 7.35E+00 I 6.20E-03 6.20E-03
X lene TH 1330207 1.48E-05 3.54E-04 1.29E-01 1.09E-04 1.09E-04

FUEL OIL COMBUSTION EMISSIONS CALCULATOR REVISION D 6/12/2008-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'tab/screen. The different tabs are on the bottom of this screen.
i�
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 is subject to continual revision and updating. It is your responsibility to be aware of the most current Information available. DENR is not
NCDENR I
responsible for errors or omissions that may be contained herein.
SOURCE/FACIUTYI USER INPUT SUMMARY FR M INPUT SCREEN
COMPANY: Perdue Farms Incorporated MAX HEAT INPUT: 20.30 MMBTU/HR
FACILITY ID NO.: 800081 FUEL HEAT VALUE: 150,000 BTU/GAL
PERMIT NUMBER: 03085T28 ACTUAL ANNUAL FUEL USAGE: 448,799 GAL/YR
FACILITY CITY: Lewiston MAXIMUM ANNUAL FUEL USAGE: 1,185,520 GAL/YR
FACILITY COUNTY: Bertie MAXIMUM SULFUR CONTENT: 2.1 %
USER NAME: Wayne Black REQUESTED PERMIT LIMITATIONS
EMISSION SOURCE DESCRIPTION: No.6 oil-fired Boiler MAX. FUEL USAGE: 1,185,520 GAL/YR
EMISSION SOURCE ID NO.: ES-5 MAX.SULFUR CONTENT: 2.1 %
TYPE OF CONTROL DEVICES POLLUTANT I CONTROL EFF.
NONE/OTHER PM 0
NONE/OTHER S02 0
NONE/OTHER NOx 0
CRITERIA AIR POLLUTANT EMISSIONS INFORMATION
ACTUAL EMISSIONS POTENTIAL EMSSIONS EMISSION FACTOR
(AFTER CONTROLS I LIMITS) (BEFORE CONTROLS I LIMITS) (AFTER CONTROLS I LIMITS) I1o/103 al
AIR POLLUTANT EMITTED Ib/hr tons/ r Ib/hr tons! r Whir tons! r uncontrolled controlled
TOTAL PARTICULATE MATTER PM FPM+CPM 3.25 5.39 3.25 14.24 3.25 14.24 2.40E+01 2.40E+01
FILTERABLE PM(FPM) 3.05 5.05 3.05 13.35 3.05 13.35 2.25E+01 2.25E+01
CONDENSABLE PM(CPM) 0.20 0.34 0.20 0.89 0.20 0.89 1.50E+00 1.50E+00
FILTERABLE PM<10 MICRONS(PM10) 2.64 4.38 2.64 11.57 2.64 11.57 1.95E+01 1.95E+01
FILTERABLE PM<2.5 MICRONS(PM2.5) 1.72 2.85 1.72 7.54 1.72 7.54 1.27E+01 1.27E+01
SULFUR DIOXIDE(S02) 44.62 73.98 44.62 195.43 44.62 195.43 3.30E+02 3.30E+02
NITROGEN OXIDES(NO,) 7.44 12.34 7.44 32.60 7.44 32.60 5.50E+01 1 5.50E+01
CARBON MONOXIDE CO 0.68 1.12 0.68 2.96 0.68 2.96 5.00E+00 5.00E+00
VOLATILE ORGANIC COMPOUNDS VOC 0.04 0.06 0.04 0.17 0.04 0.17 2.80E-01 2.80E-01
LEAD 0.00 0.00 0.00 0.00 0.00 0.00 1.51E-03 1.51 E-03
GREENHOUSE A EM1S ION /NF RMATI N
CARBON DIOXIDE(CO2) 3527.06 5848.30 3527.06 15448.51 3527.06 2.61E+04 2.61E+04
METHANE(CH4) 0.13 0.22 0.13 0.59 0.13 0.59 9.90E-01 9.90E-01
NITROUS OXIDE(N20) 0.01 0.02 0.01 0.06 0.01 0.06 1.00E-01 1.00E-01
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) (W 03 al
TOXIC I HAZARDOUS AIR POLLUTANT NUMBER Ib/hr Ib/r Whir Ib/yr Ib/hr Ib/r uncontrolled controlled
Antimony&compounds (H) SBC 7.1 E-04 2.4E+00 7.1 E-04 6.2E+00 7.1 E-04 6.2E+00 5.25E-03 5.25E-03
Arsenic&compounds (TH) ASC 1.8E-04 5.9E-01 1.8E-04 1.6E+00 1.8E-04 1.6E+00 1.32E-03 1.32E-03
Benzene (TH) 71432 2.9E-05 9.6E-02 2.9E-05 2.5E-01 2.9E-05 2.5E-01 2.14E-04 2.14E-04
Beryllium&compounds H) BEC 3.8E-06 1.2E-02 3.8E-06 3.3E-02 3.8E-06 3.3E-02 2.78E-05 2.78E-05
Cadium&compounds (TH) CDC 5.4E-05 1.8E-01 5.4E-05 4.7E-01 5.4E-05 4.7E-01 3.98E-04 3.98E-04
Chromium-AlUiotal (H) CRC 1.1E-04 3.8E-01 1.1E-04 1.0E+00 1.1E-04 1.0E+00 8.45E-04 8.45E-04
Cobalt compounds (H) CDC 8.1 E-04 2.7E+00 8.1 E-04 7.1 E+00 8.1 E-04 7.1 E+00 6.02E-03 6.02E-03
Ethylbenzene (H) 100414 8.6E-06 2.9E-02 8.6E-06 7.5E-02 8.6E-06 7.5E-02 6.36E-05 6.36E-05
Fluorides sum fluoride compounds) (T) 16984488 5.0E-03 1.7E+01 5.0E-03 4.4E+01 5.0E-03 4.4E+01 3.73E-02 3.73E-02
Formaldehyde (TH) 50000 5.8E-03 1.9E+01 5.8E-03 5.0E+01 5.8E-03 5.0E+01 4.25E-02 4.25E-02
Lead and Lead compounds (H) PBC 2.0E-04 6.8E-01 2.0E-04 1.8E+00 2.0E-04 1.8E+00 1.51E-03 1.51 E-03
Manganese&compounds (TH) MNC 4.1 E-04 1.3E+00 4.1 E-04 3.6E+00 4.1 E-04 3.6E+00 3.00E-03 3.00E-03
Mercury&Compounds (TH) HGC 1.5E-05 5.1 E-02 1.5E-05 1.3E-01 1.5E-05 1.3E-01 1.13E-04 1.13E-04
Methyl chloroform (TH) 71566 3.2E-05 1.1E-01 3.2E-05 2.8E-01 3.2E-05 2.8E-01 2.36E-04 2.36E-04
Napthalene (H) 91203 1.5E-04 5.1 E-01 1.5E-04 1.3E+00 1.5E-04 1.3E+00 1.13E-03 1.13E-03
Nickle&compounds (H) NIC 1.1E-02 3.8E+01 1.1 E-02 1.0E+02 1.1E-02 1.0E+02 8.45E-02 8.45E-02
Phos horus Metal,Yellow or White H) 7723140 1.3E-03 4.2E+00 1.3E-03 1.1E+01 1.3E-03 1.1E+01 9.46E-03 9.46E-03
POM rates uncontrolled (H) POM 1.6E-04 5.4E-01 1.6E-04 1.4E+00 1.6E-04 1.4E+00 1.20E-03 1.20E-03
Selenium compounds (H) SEC 9.2E-05 3.1 E-01 9.2E-05 8.1 E-01 9.2E-05 8.1 E-01 6.83E-04 6.83E-04
Toluene (TH) 108883 8.4E-04 2.8E+00 8.4E-04 7.4E+00 8.4E-04 7.4E+00 6.20E-03 6.20E-03
xylene (TH) 1330207 1.5E-05 4.9E-02 1.5E-05 1.3E-01 1.5E-05 1.3E-01 1.09E-04 1.09E-04
Total HAP (H) 2.2E-02 7.4E+01 2.2E-02 2.0E+02 2.2E-02 2.0E+02 1.6E-Ot 1.6E-01
Larget HAP H) 1.14E-02 3.79E+01 I 1.14E-02 1.00E+02 1.14E-02 1.00E+02 8.45E-02 8.45E-02
TOXIC AIR POLLUTANT EMISSIONS INFORMATION LFqR PERMITTING PURPOSES
EXPECTED ACTUAL EMISSIONS AFTER CONTROLS I LIMITATIONS EMISSION FACTOR
b/10' al
TOXIC AIR POLLUTANT CAS Num. Iblhr lb/day Ib/r uncontrolled controlled
Arsenic&compounds (TH) ASC 1.79E-04 4.29E-03 1.56E+00 1.32E-03 1.32E-03
Benzene (TH) 71432 2.90E-05 6.95E-04 2.54E-01 2.14E-04 2.14E-04
Cadium&compounds (TH) CDC 5.39E-05 1.29E-03 4.72E-01 3.98E-04 3.98E-04
Fluorides(sum fluoride compounds) (T) 16984488 5.05E-03 1.21E-01 4.42E+01 3.73E-02 3.73E-02
Formaldehyde (TH) 50000 5.75E-03 1.38E-01 5.04E+01 4.25E-02 4.25E-02
Manganese&compounds (TH) MNC 4.06E-04 9.74E-03 3.56E+00 3.00E-03 3.00E-03
Mercury&compounds (TH) HGC 1.53E-05 3.67E-04 1.34E-01 1.13E-04 1.13E-04
Methyl chloroform TH 71566 3.19E-05 7.67E-04 2.80E-01 2.36E-04 2.36E-04
Toluene (TH) 108883 8.39E-04 2.01E-02 7.35E+00 6.20E-03 6.20E-03
Xylene (TH) 1330207 1.48E-05 3.54E-04 1.29E-01 1.09E-04 1.09E-04

PERDUE FARMS, INC.-LEWISTON PROCESSING
5/13/2009
ACTUAL/ POTENTIAL CALCULATIONS FOR AMMONIA
PROCESS DESCRIPTION ES In Tons I Control* Ammonia Emission Ammonia Actual Ammonia Actual
LEWISTON PROCESSING # Efficien Factor(lb/ton) Emissions LB/YR EmissionsLB/HR
FUGITIVE EMISSIONS IES 77 1 7.721 1 2000 15440 1.762557078
Ammonia 15440
Total in Ibs/Yr
In Tons Year
7.72
*Efficiency Factors
15,440 pounds of Andyrous Ammonia was used in 2008.
Actual equals Potential

V
LIQUEFIED PETROLUEM GAS (LPG) COMBUSTION EMISSIONS CALCULATOR -REVISION C 10/30/2008 -OUTPUT SCREEN
Instructions: Enter emission source/facility data on the"INPUT'tab/screen. The air emission results and summary of
A�� input data are viewed/printed on the"OUTPUT'tab/screen. The different tabs are on the bottom of this screen.
Amp This spreadsheet is for your use only and should be used with caution. DENR does not guarantee the accuracy of the
NCDENR information 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
lcontamned herein
SOURCE/FACILITY/USER INPUT SUMMARY FROM INPUT SCREEN
COMPANY: Perdue Farms Incorporated FACILITY ID NO. 800081
PERMIT NUMBER: 03085T28
EMISSION SOURCE DESCRIPTION: 4.4 MMBTU/HR FIRED BOILER eys FACILITY CITY: Lewiston
EMISSION SOURCE ID NO.: ES-6,7 J FACILITY COUNTY: Bertie
SPREADSHEET PREPARED BY: Wayne Black LPG Make U
ACTUAL FUEL THROUGHPUT: 103,816 GAL/YR FUEL HEAT VALUE: 91,000 BTU/Gal Propane: 96.80
POTENTIAL FUEL THROUGHPUT: 201,143 GAL/YR BOILER TYPE: COMMERCIAL Butane: 3.20
REQUESTED MAX FUEL THRPT: 201,143 GAL/YR
CRITERIA AIR POLLUTANT EMISSIONS INFORMATION
ACTUAL EMISSIONS POTENTIAL EMSSIONS EMISSION FACTOR
(AFTER CONTROLS/LIMITS) (BEFORE CONTROLS/LIMITS) (AFTER CONTROLS/LIMITS) Ib/mmBtu
AIR POLLUTANT EMITTED Ib/hr tons/ r Ib/hr tons/ r Ib/hr tons/ r uncontrolled controlled
PARTICULATE MATTER(PM) 0.03 0.04 0.03 0.15 0.03 0.07 0.008 0.008
PARTICULATE MATTER<10 MICRONS (PM10) 0.03 0.04 0.03 0.15 0.03 0.07 0.008 0,008
PARTICULATE MATTER<2.5 MICRONS (PM25) 0.03 0.04 0.03 0.15 0.03 0.07 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 0.67 0.63 2.74 0.63 1.30 0,142 0,142
CARBON MONOXIDE(CO) 0.36 0.39 0.36 1.58 0.36 0.75 0.082 0.082
VOLATILE ORGANIC COMPOUNDS(VOC) 0.05 0.05 1 005 021 0.05 0.10 1 0.011 0.011
TOXIC/HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION
ACTUAL EMISSIONS POTENTIAL EMSSIONS EMISSION FACTOR
CAS (AFTER CONTROLS/LIMITS) (BEFORE CONTROLS/LIMITS) (AFTER CONTROLS/LIMITS) Ib/mmBtu
TOXIC I HAZARDOUS AIR POLLUTANT NUMBER Ib/hr tons/yr Ib/hr tons/yr Ib/hr tons/yr uncontrolled controlled
TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR PERMITTING PURPOSES
EXPECTED ACTUAL EMISSIONS AFTER CONTROLS/LIMITATIONS EMISSION FACTOR
Ib/mmBtu
TOXIC AIR POLLUTANT CAS Nunn Ib/hr lb/day Ib/yr uncontrolled controlled
GREENHOUSE GAS POLLUTANT EMISSIONS INFORMATION(FOR EMISSION INVENTORY PURPOSES)
ACTUAL EMISSIONS POTENTIAL EMISSIONS EMISSION FACTOR
,AFTER CONTROLS/LIMITS) (BEFORE CONTROLS/LIMITS) (AFTER CONTROLS/LIMITS) b/nI
GREENHOUSE GAS POLLUTANT Ib/hr tons/yr Ib/hr tons/yr Ib/hr tons/yr uncontrolled controlled
CARBON DIOXIDE 609.63 654.47 609.63 2670.17 609.63 1268.03 138.55 138.55
METHANE 0.01 0.01 0.01 0.04 0.01 0.02 0.0020 0.0020
NITROUS OXIDE 0.04 0.04 0.04 0.17 0.04 0.08 0.0088 0.0088

NATURAL GAS COMBUSTION EMISSIONS CALCULATOR REVISION F 10/31/2008-OUTPUT SCREEN
Instructions: Enter emission source/facility data on the"INPUT"tab/screen. 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.
,.f 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 is subject to continual revision and updating. It is your responsibility to be aware of the most current information available.
NCDENRDENR is not responsible for errors or omissions that may be contained herein.
COMPANY: Perdue Farms Incorporated FACILITY ID NO.: 800 81
PERMIT NUMBER: 03085T28
EMISSION SOURCE DESCRIPTION: 84 MMBTU/HR NATURAL GAS-FIRED BOILER FACILITY CITY: Lewiston
EMISSION SOURCE ID NO.: ES-8 FACILITY COUNTY: Bertie
CONTROL DEVICE: I NO CONTROL POLLUTANT CONTROL EFF.
SPREADSHEET PREPARED BY: Wayne Black NOX CALC'D AS 0%
ACTUAL FUEL THROUGHPUT: 251.00 10 SCF/YR FUEL HEAT VALUE: 1,029 BTU/SCF
POTENTIAL FUEL THROUGHPUT: 715.10 10 SCFNRI BOILER TYPE: SMALL BOILER <100 mmBTU/HR
REQUESTED MAX.FUEL THRPT: 715.10 10 SCF/YR NO SNCR APPLIED
CRITERIA AIR POLLUTANTEMISSIONS INFORMATION
ACTUAL EMISSIONS POTENTIAL EMSSIONS EMISSION FACTOR
(AFTER CONTROLS/LIMITS) (BEFORE CONTROLS/LIMITS) (AFTER CONTROLS/LIMITS) Ib/mmBtu
AIR POLLUTANT EMITTED Ib/hr tons/ r Whir tons/ r Ib/hr tons/ r uncontrolled controlled
PARTICULATE MATTER(Total) 0.62 0.95 0.62 2.72 0.62 2.72 0.007 0.007
PARTICULATE MATTER Condensable 0.47 0.72 0.47 2.04 0.47 2.04 0.006 0.006
PARTICULATE MATTER Filterable 0.16 0.24 0.16 0.68 0.16 0.68 0.002 0.002
SULFUR DIOXIDE S02 0.05 0.081 0.05 0.21 0.05 0.211 0.001 0,001
NITROGEN OXIDES NOx 8.16 12.551 8.16 35.76 8.16 3d76 0.097 0.097
CARBON MONOXIDE CO 6.86 10.5416.86 30.03 6.86 3 0.082 0.082
VOLATILE ORGANIC COMPOUNDS OC 0.45 0,69 0.45 1.97 OA5 0.005 0.005
LEAD 4.08E-OS 6.3E-05 4.1 E-05 1.8E-04 4.1 E-05 1.8 4.9E-07 4.9E-07
TOXIC/HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION
ACTUAL EMISSIONS POTENTIAL EMSSIONS EMISSION FACTOR
CAS (AFTER CONTROLS/LIMITS) (BEFORE CONTROLS/LIMITS) (AFTER CONTROLS/LIMITS) Ib/mmBtu
TOXIC I HAZARDOUS AIR POLLUTANT NUMBER Ib/hr Ibs/r Ib/hf Ibs/ r Whir Ibs/ r uncontrolled controlled
Arsenic&Compounds H ASC 0.00E+00 O.00E+00 0.00E+00 0.00E+00 0.00E+00 O.00E+00 0.00E+00 0.oOE+00
Benzene H 71432 1.71 E-04 5.27E-01 1.71E-04 1.50E+00 1.71 E-04 1.50E+00 2.04E-06 2.04E-06
Benzo a rene H 50328 9.80E-08 3.01 E-04 9.80E-08 8.58E-04 9.80E-08 8.58E-04 1.17E-09 1.17E-09
Beryllium metal TH 7440417 0.00E+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+00 0.00E+00 O.o0E+00 0.00E+00 0.00E+00 O.00E+OO
Chromium-All/Total H CRC 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 I 0.00E+00 0.00E+00 O.00E+00
Soluble Chromate Compounds,as Chromium I H SoICR6 0.00E+00 O.00E+00 0.00E+00 O.00E+00 O.00E+00 0.00E+00 0.00E+00 O.o0E+00
Cobalt compounds H CDC 6.86E-06 2.11 E-02 6.86E-06 6.01E-02 6.86E-06 6.01 E-02 8.16E-08 8.16E-08
Formaldehyde H 50000 6.12E-03 1.88E+01 6.12E-03 5.36E+01 6.12E-03 5.36E+01 7.29E-05 7.29E-05
Hexane,n- H 110543 1.47E-01 4.52E+02 1.47E-01 1.29E+03 1.47E-01 1.29E+03 1.75E-03 1.75E-03
Manganese&compounds TH MNC 0.00E+00 O.00E+00 0.00E+00 0.00E+00 O.00E+00 O.00E+00 O.00E+00 O.00E+OO
Mercury &Compounds H HGC 0.00E+00 0.00E+00 0.00E+00 O.00E+00 O.00E+00 0.00E+00 0.00E+00 0.00E+00
Na thalene H 91203 4.98E-05 1.53E-01 4.98E-05 4.36E-01 4.98E-05 4.36E-01 5.93E-07 5.93E-07
Nickel metal H 7440020 0.00E+00 1 0.00E+00 1 O.00E+00 1 0.00E+00 O.00E+00 I O.00E+00 1 0.00E+00 0.00E+00
Selenium compounds H SEC 1.96E-06 I 6.02E-03 I 1.96E-06 I 1.72E-02 1.96E-06 I 1.72E-02 I 2.33E-08 2.33E-08
Toluene H 108883 2.78E-04 8.53E-01 2.78E-04 2.43E+00 2.78E-04 I 2.43E+00 I 3.30E-06 3.30E-06
Total HAPs 1.54E-01 4.72E+02 1.54E-01 1.35E+03 1.54E-01 I 1.35E+03 I 1.83E-03 1.83E-03
Highest HAP Hexane 1.47E-01 4.52E+02 1.47E-01 1.29E+03 I 1.47E-01 1 1.29E+03 1.75E-03 1.75E-03
TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR 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 H ASC 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00
Benzene H 71432 1.71E-04 4.11 E-03 1.50E+00 2.04E-06 2.04E-06
Benzo a rene H 50328 9.80E-08 2.35E-06 8.58E-04 117E-09 1.17E-09
Beryllium metal H 7440417 0.00E+00 0.00E+00 0.00E+00 0.00E+00 O.00E+00
Cadmium&compounds TH CDC 0.00E+00 0.00E+00 0.00E+00 O.00E+00 O,OOE+oO
Soluble Chromate Compounds,as Chromium I H SoICR6 0.00E+00 0.00E+00 0.00E+00 0.00E+00 O.00E+00
Formaldehyde H 50000 6.12E-03 1.47E-01 5.36E+01 7.29E-05 7.29E-05
Hexane,n- H 110543 1.47E-01 3.53E+00 1.29E+03 1.75E-03 1.75E-03
Manganese&compounds H MNC 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00
Mercury &Compounds H HGC 0.00E+00 0.00E+00 0.00E+00 0.00E+00 O.00E+oO
Nickel metal TH 7440020 0.00E+00 0.00E+00 0.00E+00 O.o0E+00 O.00E+oO
Toluene(TH) 108883 2.78E-04 6.66E-03 2.43E+00 3.30E-06 3.30E-06
GREENHOUSE GAS --I- - WAMM(FOR EMISSIONS
ACTUAL EMISSIONS POTENTIAL EMISSIONS Emission Factor
(AFTER CONTROLS I LIMITS) (BEFORE CONTROLS I LIMITS) (AFTER CONTROLS/LIMITS) Ib/mmBtu
GREENHOUSE GAS POLLUTANT Ib/hf I tons/yf Ib/hr tons/yf Ib/hf I tons/yr uncontrolled I controlled
Carbon Dioxide 9825.311 15105.18 9825.31 43034.85 9825.311 43034.85 116.971 116.97
Methane 0.1671 2.56E-01 0.167 7.30E-01 0.1671 7.30E-01 1.98E-03 1.98E-03
Nitrous oxide 0.1671 2.56E-01 0.167 7.30E-01 0.1671 7.30E-01 1.98E-03 1.98E-03

1
FUEL OIL COMBUSTION EMISSIONS CALCULATOR REVISION D 6/12/2008-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'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 is subject to continual revision and updating. It is your responsibility to be aware of the most current Information available. DENR Is not
NCDENRresponsible for errors or omissions that may be contained herein.
SOURCE/FACILITY/USER INPUT SUMMARY FROM INPUT SCREEN
COMPANY: Perdue Farms Incorporated MAX HEAT INPUT: 84.00 MMBTU/HR
FACILITY ID NO.: 800081 FUEL HEAT VALUE: 150,000 BTU/GAL
PERMIT NUMBER: 03085T28 ACTUAL ANNUAL FUEL USAGE: 147,956 GAL/YR
FACILITY CITY: Lewiston MAXIMUM ANNUAL FUEL USAGE: 4,905,600 GAUYR
FACILITY COUNTY: Bertie MAXIMUM SULFUR CONTENT 18 %
USER NAME: Wayne Black REQUESTED PERMIT LIMITATIONS
EMISSION SOURCE DESCRIPTION: No.6 oil-fired Boiler MAX FUEL USAGE 4,905.600 GAL/YR
EMISSION SOURCE ID NO ES-8 MAX SULFUR CONTENT 1.8 %
TYPE OF CONTROL DEVICES POLLUTANT CONTROL EFF.
NONE/OTHER PM 45
NONE/OTHER S02 56.8
NONE/OTHER NOx 0
CRITERIA AIR POLLUTANT EMISSIONS INFORMATION
ACTUAL EMISSIONS POTENTIAL EMSSIONS EMISSION FACTOR
(AFTER CONTROLS/LIMITS) (BEFORE CONTROLS/LIMITS) (AFTER CONTROLS/LIMITS) Ib110' al
AIR POLLUTANT EMITTED Ib/hr tons/ r Ib/hr tons/ r Ib/hr tons/ r uncontrolled controlled
TOTAL PARTICULATE MATTER PM FPM+CPM 6.55 0.87 11.91 52.15 6.55 28.68 2.13E+01 1.17E+01
FILTERABLE PM(FPM) 6.09 0.80 11.07 48.47 6.09 26.66 1.98E+01 1.09E+01
CONDENSABLE PM(CPM) 0.46 0.06 0.84 3.68 0.46 2.02 1.50E+00 8.25E-01
FILTERABLE PM<10 MICRONS(PM10) 5.27 0.70 9.58 41.96 5.27 23.08 1.71E+01 9.41E+00
FILTERABLE PM<2.5 MICRONS(PM2.5) 3.43 0.45 6.24 27.33 3.43 15.03 1.11E+01 6.13E+00
SULFUR DIOXIDE(SO,) 68.37 9.03 158.26 693.16 68.37 299.45 2.83E+02 1.22E+02
NITROGEN OXIDES(NO.) 30.80 4.07 30.80 134.90 30.80 134.90 5.50E+01 5.50E+01
CARBON MONOXIDE CO 2.80 0.37 2.80 12.26 2.80 12.26 5.00E+00 5.00E+00
VOLATILE ORGANIC COMPOUNDS VOC 0.16 0.02 0.16 0.69 0.16 0.69 2.80E-01 2.80E-01
LEAD 0,00 0.00 000 000 000 000 1,51E-03 8 31E-04
GREENHOUSE GAS EMISSIONS INFORMATION
CARBON DIOXIDE(CO2) 14594 72 192801 14594.72 63924,87 14594.72 // # 2 61E+04 2 61E+04
METHANE(CH4) 0.55 0.07 0.55 2.43 0.55 2.43 9.90E-01 9.90E-01
NITROUS OXIDE(N20) 0,06 0,01 1 0.06 0.25 0 06 0.25 1.00E-01 1.00E-01
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/103 al
TOXIC I HAZARDOUS AIR POLLUTANT NUMBER Iblhr Ib/r Ib/hr Ib/r Ib/hr Iblyr uncontrolled controlled
Antimony&compounds (H) SBC 1.6E-03 4.3E-01 2.9E-03 2.6E+01 1.6E-03 1.4E+01 5.25E-03 2.89E-03
Arsenic&compounds ITT) ASC 4.1 E-04 1.1E-01 7.4E-04 6.5E+00 4.1 E-04 3.6E+00 1.32E-03 7.26E-04
Benzene ITT) 71432 1.2E-04 3.2E-02 1.2E-04 1.0E+00 1.2E-04 1.0E+00 2.14E-04 2.14E-04
Beryllium&compounds (H) BEC 8.6E-06 2.3E-03 I 1.6E-05 1.4E-01 8.6E-06 7.5E-02 2.78E-05 1.53E-05
Cadium&compounds TH CDC 1.2E-04 3.2E-02 2.2E-04 2.0E+00 1.2E-04 1.1 E+00 3.98E-04 2.19E-04
Chromium-AII/Total H CRC 2.6E-04 6.9E-02 4.7E-04 4.1E+00 2.6E-04 2.3E+00 8.45E-04 4.65E-04
Cobalt compounds H) CDC 1.9E-03 4.9E-01 3.4E-03 3.0E+01 1.9E-03 1.6E+01 6.02E-03 3.31E-03
Eth(benzene (H 100414 3.6E-05 94E-03 3.6E-05 3.1 E-01 3.6E-05 3.1 E-01 6.36E-05 6.36E-05
Fluorides sum fluoride compounds) (T 16984488 2.1 E-02 5.5E+00 2.1 E-02 1.8E+02 2.1 E-02 1.8E+02 3.73E-02 3.73E-02
Formaldehyde (TH) 50000 24E-02 6.3E+00 24E-02 2.1E+02 24E-02 2.1E+02 4.25E-02 4.25E-02
Lead and Lead compounds (H) PBC 4.7E-04 1.2E-01 8.5E-04 7.4E+00 4.7E-04 4.1 E+00 1.51E-03 8.31 E-04
Manganese&compounds (TH) MNC 9.2E-04 24E-01 1.7E-03 1.5E+01 9.2E-04 8.1 E+00 3.00E-03 1.65E-03
Mercury&compounds (TH) HGC 6.3E-05 1.7E-02 6.3E-05 5.5E-01 6.3E-05 5.5E-01 1.13E-04 1.13E-04
Methyl chloroform (TH) 71566 1.3E-04 3.5E-02 1.3E-04 1.2E+00 1.3E-04 1.2E+00 2.36E-04 2.36E-04
Na thalene (IT) 91203 6.3E-04 1.7E-01 6.3E-04 5.5E+00 6.3E-04 5.5E+00 113E-03 1.13E-03
Nickle&compounds (H) NIC 2.6E-02 6.9E+00 4 7E-02 4.1 E+02 2.6E-02 2.3E+02 845E-02 4.65E-02
Phosphorus Metal,Yellow or White (H) 7723140 2.9E-03 7.7E-01 5.3E-03 4.6E+01 2.9E-03 2.6E+01 9.46E-03 5.20E-03
POM rates uncontrolled (H) POM 3.7E-04 9.8E-02 6.7E-04 5.9E+00 3.7E-04 3.2E+00 1.20E-03 6.60E-04
Selenium compounds (H) SEC 2.1E-04 5.6E-02 3.8E-04 3.4E+00 2.1E-04 1.8E+00 6.83E-04 3.76E-04
Toluene (TH) 108883 3.5E-03 9.2E-01 3.5E-03 3.0E+01 3.5E-03 3.0E+01 6.20E-03 6.20E-03
X lane TH 1330207 6.1E-05 1.6E-02 6.1E-05 5.3E-01 6.1E-05 5.3E-01 1.09E-04 1.09E-04
Total HAP H) 6.3E-02 1.7E+01 9.2E-02 8.1E+02 6.3E-02 5.6E+02 1.6E-01 1.1E-01
Lar et HAP (IT) 2.60E-02 6.88E+00 4.73E-02 4.15E+02 2.60E-02 2.28E+02 8.45E-02 4.65E-02
TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR PERMITTING PURPOSES
EXPECTED ACTUAL EMISSIONS AFTER CONTROLS/LIMITATIONS EMISSION FACTOR
(Ib/103 al
TOXIC AIR POLLUTANT CAS Num. Ib/hr lb/day lbtyr uncontrolled controlled
Arsenic&compounds (TH) ASC 4.07E-04 9.76E-03 3.56E+00 1.32E-03 7.26E-04
Benzene TH 71432 1.20E-04 2.88E-03 1.05E+00 2.14E-04 2.14E-04
Cadium&compounds (TH) CDC 1.23E-04 2.94E-03 1.07E+00 3.98E-04 2.19E-04
Fluordes sum fluoride compounds) T 16984488 2.09E-02 5.01E-01 1.83E+02 3.73E-02 3.73E-02
Formaldehyde (TH) 50000 2.38E-02 5.71E-01 2.08E+02 4.25E-02 4.25E-02
Manganese&compounds (TH) MNC 9,24E-04 2.22E-02 8.09E+00 3.00E-03 1.65E-03
Mercury&Compounds TH HGC 6.33E-05 1.52E-03 5.54E-01 1.13E-04 1.13E-04
Meth I chloroform TH 71566 1.32E-04 3.17E-03 1.16E+00 2.36E-04 2.36E-04
Toluene TH 108883 3.47E-03 8.33E-02 3.04E+01 6.20E-03 6.20E-03
X lene TH 1330207 6.10E-05 1.46E-03 5.35E-01 1.09E-04 1.09E-04

NATURAL GAS COMBUSTION EMISSIONS CALCULATOR REVISION F 10/31/2008-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"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 is subject to continual revision and updating. It is your responsibility to be aware of the most current information available.
NCDENRDENR is not responsible for errors or omissions that may be contained herein.
TUOWI INPUT SUMMA M
COMPANY: Perdue Farms Incorporated 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 CONTROL EFF.
SPREADSHEET PREPARED BY: Wayne Black NOX CALC'D AS 0%
ACTUAL FUEL THROUGHPUT: 251.00 10 SCF/YR FUEL HEAT VALUE: 1,029 BTU/SCF
POTENTIAL FUEL THROUGHPUT: 715.10 106 SCFNRI BOILER TYPE: SMALL BOILER <100 mmBTU/HR
REQUESTED MAX.FUEL THRPT: 715.10 10 SCFNR NO SNCR APPLIED
CRITERIA AIR POLLUTANTENISSIONS MWORMATM
ACTUAL EMISSIONS POTENTIAL EMSSIONS EMISSION FACTOR
(AFTER CONTROLS I LIMITS) (BEFORE CONTROLS/LIMITS) (AFTER CONTROLS/LIMITS) Ib/mm Btu
AIR POLLUTANT EMITTED Ib/hr tons/ r Ib/hr tons r Ib/hr tonstyr uncontrolled controlled
PARTICULATE MATTER Total 0.62 0.95 0.62 2.72 0.62 2.72 0.007 0.007
PARTICULATE MATTER Condensable 0.47 0.72 0.47 2.04 0.47 2.04 0.006 0.006
PARTICULATE MATTER Filterable 0.16 0.24 0.16 0.68 0.16 0.68 0,002 0.002
SULFUR DIOXIDE S02 0.05 0.08 0.05 0.21 0.05 0.21 0.001 0.001
NITROGEN OXIDES NOx 8.16 12.55 8.16 35.76 8.16 35.76 0.097 0.097
CARBON MONOXIDE CO 6.86 10.54 6.86 30.03 6.86 30.03 0.082 0.082
VOLATILE ORGANIC COMPOUNDS OC 0% 0.69 0.45 1.97 0.45 1.97 0.0051 0.005
LEAD 4.08E-05 6.3E-05 4.1 E-051 1.8E-04 4.1E-05 1.8E-04 4.9E-07 4.9E-07
TOXIC/HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION
ACTUAL EMISSIONS POTENTIAL EMSSIONS EMISSION FACTOR
CAS (AFTER CONTROLS/LIMITS) (BEFORE CONTROLS/LIMITS) (AFTER CONTROLS/LIMITS) Ib/mmBtu
TOXIC I HAZARDOUS AIR POLLUTANT NUMBER Ib/hr Ibs/r Ib/hr Ibs/ r Ib/hr Ibs/ r uncontrolled Controlled
Arsenic&Compounds TH ASC 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 O.00E+00 0.00E+00
Benzene H 71432 1.71E-04 5.27E-01 1.71 E-04 1.50E+00 1.71E-04 1.50E+00 2.04E-06 2.04E-06
Benzo a rene H 50328 9.80E-08 3.01 E-04 9.80E-08 8.58E-04 9.80E-08 8.58E-04 1.17E-09 1 17E-09
Beryllium metal H 7440417 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 O.00E+00 000E+00
Cadmium&compounds TH CDC 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 O.o0E+00 O.00E+00
Chromium-All/Total H CRC 0.00E+00 O.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 O.00E+00 O.00E+OO
Soluble Chromate Compounds,as Chromium I H SoICR6 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 O.00E+00 O.00E+00
Cobalt compounds H COC 6.86E-06 2.11 E-02 6.86E-06 6.01E-02 6.86E-06 6.01 E-02 8.16E-08 8 16E-08
Formaldehyde H 50000 6.12E-03 1.88E+01 6.12E-03 5.36E+01 6.12E-03 5.36E+01 7.29E-05 7.29E-05
Hexane,n- TH 110543 1.47E-01 4.52E+02 1.47E-01 1.29E+03 1.47E-01 1.29E+03 1.75E-03 1.75E-03
Manganese&compounds TH MNC 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 O.00E+00
Mercury &Compounds TH HGC 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 O.00E+00 O.00E+00
Na thalene H 91203 4.98E-05 1.53E-01 4.98E-05 4.36E-01 4.98E-05 4.36E-01 5.93E-07 5.93E-07
Nickel metal H 7440020 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 O.00E+00 0.00E+00
Selenium compounds H SEC 1.96E-06 6.02E-03 1.96E-06 1.72E-02 1.96E-06 1.72E-02 233E-08 2.33E-08
Toluene H 108883 2.78E-04 8.53E-01 2.78E-04 2.43E+00 2.78E-04 2.43E+00 3.30E-06 3.30E-06
Total HAPs 1.54E-01 I 4.72E+02 1.54E-01 I 1.35E+03 1.54E-01 1.35E+03 1.83E-03 1.83E-03
Highest HAP IHexane I 1.47E-01 I 4.52E+02 I 1.47E-01 I 1.29E+03 I 1.47E-01 I 1.29E+03 1.75E-03 1.75E-03
TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR PERMITTING PURPOSES
EXPECTED ACTUAL EMISSIONS AFTER CONTROLS I LIMITATIONS EMISSION FACTOR
Ib/mmetu
TOXIC AIR POLLUTANT CAS Num. Ib/hr lb/day Ib/ r uncontrolled controlled
Arsenic&Compounds H ASC 0.00E+00 0.00E+00 0.00E+00 0 00E+00 O.00E+00
Benzene TH 71432 1.71 E-04 4.11 E-03 1.50E+00 2.04E-06 2.04E-06
Benzo a rene TH 50328 9.80E-08 2.35E-06 8.58E-04 1.17E-09 1.17E-09
Beryllium metal TH 7440417 0.00E+00 0.00E+00 0.00E+00 O.00E+00 O.oOE+OO
Cadmium&compounds TH CDC 0.00E+00 0.00E+00 0.00E+00 O.00E+00 O.o0E+00
Soluble Chromate Compounds,as Chromium I TH SoICR6 0.00E+00 0.00E+00 0.00E+00 O.00E+OO O.00E+00
Formaldehyde H 50000 6.12E-03 1.47E-01 5.36E+01 7.29E-05 7.29E-05
Hexane,n- H 110543 1.47E-01 3.53E+00 1.29E+03 1.75E-03 1.75E-03
Manganese&compounds H MNC 0.00E+00 0.00E+00 0.00E+00 O.00E+00 O.00E+00
Mercury &Compounds H HGC 0.00E+00 0.00E+00 0.00E+00 o.00E+00 O.00E+00
Nickel metal H 7440020 0.00E+00 0.00E+00 0.00E+00 0.00E+00 O.00E+00
Toluene(TH) 108883 2.78E-04 6.66E-03 2.43E+00 3.30E-06 3.30E-06
ACTUAL EMISSIONS POTENTIAL EMISSIONS Emission Factor
(AFTER CONTROLS I LIMITS) (BEFORE CONTROLS I LIMITS) (AFTER CONTROLS I LIMITS) Ib/mmBtu
GREENHOUSE GAS POLLUTANT Ib/hr I tons/yr Ib/hr tons/yr Ib/hr tons/yr uncontrolled I controlled
Carbon Dioxide 9825.311 15105.18 9825.31 43034.85 9825.31 43034.85 116.97 116.97
Methane 0.1671 2.56E-01 0,167 7.30E-01 0.167 7.30E-01 1.98E-03 1.98E-03
Nitrous oxide 0.1671 2.56E-01 0.167 7.30E-01 0.167 7.30E-01 1.98E-03 1.98E-03

1
FUEL OIL COMBUSTION EMISSIONS CALCULATOR REVISION D 6/12/2008-OUTPUT SCREEN
Instructions: Enter emission source/facility data on the'INPUT"tab/screen. The air emission results and summary of
ATWA input data are viewed/printed on the"OUTPUT'tab/screen. The different tabs are on the bottom of this screen.
-t 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 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.
NCDENR
SOURCE/FACILITY/USER INPUT SUMMARY INPUT SCREEN
COMPANY: Purdue Farms Incorporated MAX HEAT INPUT: 84.00 MMBTU/HR
FACILITY ID NO.: 800081 FUEL HEAT VALUE: 150,000 BTU/GAL
PERMIT NUMBER: 03085T28 ACTUAL ANNUAL FUEL USAGE: 147,956 GAL/YR
FACILITY CITY: Lewiston MAXIMUM ANNUAL FUEL USAGE: 4,905,600 GAL/YR
FACILITY COUNTY: Bertie MAXIMUM SULFUR CONTENT: 1.8 %
USER NAME: Wayne Black REQUESTED PERMIT LIMITATIONS
EMISSION SOURCE DESCRIPTION: No.6 oil-fired Boiler MAX. FUEL USAGE: 4,905,600 GAL/YR
EMISSION SOURCE ID NO.: ES-9 MAX.SULFUR CONTENT: 1.84 %
TYPE OF CONTROL DEVICES POLLUTANT CONTROL EFF.
NONE/OTHER PM 45
NONE/OTHER S02 56.8
NONE/OTHER NOx 0
CRITERIA AIR POLLUTANT EMISSIONS INFORMATION
ACTUAL EMISSIONS POTENTIAL EMSSIONS EMISSION FACTOR
(AFTER CONTROLS/LIMITS) (BEFORE CONTROLS/LIMITS) (AFTER CONTROLS/LIMITS) (lb/103gal)
AIR POLLUTANT EMITTED Ib/hr tons/ r Whir tons/ r Ib/hr tons/ r uncontrolled controlled
TOTAL PARTICULATE MATTER PM FPM+CPM 6.55 0.87 11.91 52.15 6.55 28.68 2.13E+01 1.17E+01
FILTERABLE PM(FPM) 6.09 0.80 11.07 48.47 6.09 26.66 1.98E+01 1.09E+01
CONDENSABLE PM(CPM) 0.46 0.06 0.84 3.68 0.46 2.02 1.50E+00 8.25E-01
FILTERABLE PM<10 MICRONS(PM10) 5.27 0.70 9.58 41.96 5.27 23.08 1.71E+01 9.41E+00
FILTERABLE PM<2.5 MICRONS(PM2.5) 3.43 0.45 6.24 27.33 3.43 15.03 1.11E+01 6.13E+00
SULFUR DIOXIDE(S02) 68.37 9.03 158.26 693.16 69.89 306.10 2.83E+02 1.22E+02
NITROGEN OXIDES(NO.) 30.80 4.07 30.80 134.90 30.80 134.90 5.50E+01 5.50E+01
CARBON MONOXIDE CO 2.80 0.37 2.80 12.26 2.80 12.26 5.00E+00 5.00E+00
VOLATILE ORGANIC COMPOUNDS VOC 0.16 0.02 0.16 0.69 0.16 0.69 2.80E-01 2.80E-01
LEAD 0.00 0.00 0.00 0.00 000 0.00 1.51 E-03 8.31 E-04
GREENHOUSEA EMISSIONS N MAT/ IN
CARBON DIOXIDE(CO2) 14594.72 1928.01 14594.72 63924.87 14594.72 2.61E+04 2.61E+04
METHANE(CH4) 0.55 0.07 0.55 2.43 0.55 2.43 9.90E-01 9.90E-01
NITROUS OXIDE(N20) 0.06 0.01 1 0.06 0.25 0.06 0.25 1.00E-01 1.00E-01
TOXIC/HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION
ACTUAL EMISSIONS POTENTIAL EMSSIONS EMISSION FACTOR
CAS (AFTER CONTROLS/LIMITS) (BEFORE CONTROLS/LIMITS) (AFTER CONTROLS I LIMITS) Ib/103 al
TOXIC/HAZARDOUS AIR POLLUTANT NUMBER Ib/hr lbtyr Ib/hr Ib/r Ib/hr Ib/r uncontrolled controlled
Antimony&compounds (IT) SEC 1.6E-03 4.3E-01 2.9E-03 2.6E+01 1.6E-03 1.4E+01 5.25E-03 2.89E-03
Arsenic&compounds (TH) ASC 4.1E-04 1.1E-01 7.4E-04 6.5E+00 4.1 E-04 3.6E+00 1.32E-03 7.26E-04
Benzene (TH) 71432 1.2E-04 3.2E-02 1.2E-04 1.0E+00 1.2E-04 1.0E+00 2.14E-04 2.14E-04
Beryllium&compounds H) BEC 8.6E-06 2.3E-03 1.6E-05 1.4E-01 8.6E-06 7.5E-02 2.78E-05 1.53E-05
Cadium&compounds (TH) CDC 1.2E-04 3.2E-02 2.2E-04 2.0E+00 1.2E-04 1.1 E+00 3.98E-04 2.19E-04
Chromium-AII/rotal (H) CRC 2.6E-04 6.9E-02 4.7E-04 4.1E+00 2.6E-04 2.3E+00 I 8.45E-04 4.65E-04
Cobalt compounds (H) CDC 1.9E-03 4.9E-01 3.4E-03 3.0E+01 1.9E-03 1.6E+01 6.02E-03 3.31 E-03
Eth(benzene (H) 100414 3.6E-05 9.4E-03 3.6E-05 3.1 E-01 3.6E-05 3.1 E-01 6.36E-05 6.36E-05
Fluorides(sum fluoride compounds) (T) 16984488 2.1 E-02 5.5E+00 2.1 E-02 1.8E+02 2.1 E-02 1.8E+02 3.73E-02 3.73E-02
Formaldehyde (TH) 50000 2.4E-02 6.3E+00 2.4E-02 2.1E+02 2.4E-02 2.1E+02 4.25E-02 4.25E-02
Lead and Lead compounds (H) PBC 4.7E-04 1.2E-01 8.5E-04 7.4E+00 4.7E-04 4.1 E+00 1.51 E-03 8.31 E-04
Manganese&compounds (TH) MNC 9.2E-04 2.4E-01 1.7E-03 1.5E+01 9.2E-04 8.1 E+00 3.00E-03 1.65E-03
Mercury&compounds (TH) HGC 6.3E-05 1.7E-02 6.3E-05 5.5E-01 6.3E-05 5.5E-01 1.13E-04 1.13E-04
Methyl chloroform (TH) 71566 1.3E-04 3.5E-02 1.3E-04 1.2E+00 1.3E-04 1.2E+00 2.36E-04 2.36E-04
Napthalene (H) 91203 6.3E-04 1.7E-01 6.3E-04 5.5E+00 6.3E-04 5.5E+00 1.13E-03 1.13E-03
Nickle&Compounds (H) NIC 2.6E-02 6.9E+00 4.7E-02 4.1 E+02 2.6E-02 2.3E+02 8.45E-02 4.65E-02
Phosphorus Metal,Yellow or White (H) 7723140 2.9E-03 7.7E-01 5.3E-03 4.6E+01 2.9E-03 2.6E+01 9.46E-03 5.20E-03
POM rates uncontrolled (H) POM 3.7E-04 9.8E-02 6.7E-04 5.9E+00 3.7E-04 3.2E+00 1.20E-03 6.60E-04
Selenium compounds (H SEC 2.1 E-04 5.6E-02 3.8E-04 3.4E+00 2.1 E-04 1.8E+00 6.83E-04 3.76E-04
Toluene (TH) 108883 3.5E-03 9.2E-01 3.5E-03 3.0E+01 3.5E-03 3.0E+01 6.20E-03 6.20E-03
X lene (TH) 1330207 6.1 E-05 1.6E-02 6.1 E-05 5.3E-01 6.1 E-05 5.3E-01 1.09E-04 1.09E-04
Total HAP (H) 6.3E-02 1.7E+01 92E-02 8.1E+02 6.3E-02 5.6E+02 1.6E-01 1.1E-01
Lar et HAP (H) 2.60E-02 6.88E+00 4.73E-02 4.15E+02 2.60E-02 2.28E+02 8.45E-02 4.65E-02
TOXIC AIR POLLUTANT EMISSIONS INFORMATION LFOR PERMITTING PURPOSES
EXPECTED ACTUAL EMISSIONS AFTER CONTROLS I LIMITATIONS EMISSION FACTOR
Ib/103 al
TOXIC AIR POLLUTANT CAS Num. Ib/hr lb/day Ib/r uncontrolled 1controlled
Arsenic&compounds (TH) ASC 4.07E-04 9.76E-03 3.56E+00 1.32E-03 7.26E-04
Benzene (TH) 71432 1.20E-04 2.88E-03 1.05E+00 2.14E-04 2.14E-04
Cadium&compounds (TH) CDC 1.23E-04 2.94E-03 1.07E+00 3.98E-04 2.19E-04
Fluorides(Sum fluoride compounds) (T) 16984488 2.09E-02 5.01E-01 1.83E+02 3.73E-02 3.73E-02
Formaldehyde (TH) 50000 2.38E-02 5.71E-01 2.08E+02 4.25E-02 4.25E-02
Manganese&compounds (TH) MNC 9.24E-04 2.22E-02 8.09E+00 3.00E-03 1.65E-03
Mercury&compounds TH HGC 6.33E-05 1.52E-03 5.54E-01 1.13E-04 1.13E-04
Methyl chloroform TH 71566 1.32E-04 3.17E-03 1.16E+00 2.36E-04 2.36E-04
Toluene (TH) 108883 3.47E-03 8.33E-02 3.04E+01 6.20E-03 6.20E-03
X lene (TH) 1330207 6.10E-05 1.46E-03 5.35E-01 1.09E-04 1.09E-04

PERDUE FARMS,INC.
C� � � ��� lno
!�
r� off ►�°
�
I J
ACTUAL/POTENTIAL CALCULATIONS FOR GHG METHANE (CH4)
Wastewater Flow(gallons) ✓
COD Conentration Mg/1 V 6"1 ��i l IJU C
PROCESS DESCRIPTION ES Control' COD Value Methant Emission Methane Actual
Anaerobic Ponds # Flow M Efficiency (K M' Factor(Kg C g COD) Methane Fraction Emissions(Kg/Year)
FUGITIVE EMISSIONS Ana 1 1 302,348 1 1 5.722 0.25 0.8 346,007
Methane Total in Metric 346
Tons
Methane Total in Short 381
Tons
ACTUAL/POTENTIAL CALCULATIONS FOR GHG METHANE (CH4)
Wastewater Flow(gallons)
COD Conentration Mg/I
PROCESS DESCRIPTION ES 3 Control' COD Value Methane Emission Methane Actual
Flow M 3 Methane Fraction
Anaerobic Ponds
Efficiency (K M Factor(Kg CH4/Kg COD) Emissions(Kg/Year)
FUGITIVE EMISSIONS Ana 2 2,933,150 1 2.641 0.25 0.8 1,549,290
Methane Total in Metric 1549
Tons
Methane Total in Short 1,704
Tons
1

HnnoQp m( % ol
Drinking Water ID: 37715 III
Wastewater ID: 10
P.O. BOX 7085, 114 OAKMONT DRIVE PHONE (252) /bb-6208
GREENVILLE, N.C. 27835-7085 FAX [phone]
ID#: 233 Z
PERDUE FARMS, INC. (LEWISTON)
MR. WAYNE BLACK
P.O. BOX 460 DATE COLLECTED: 05/27/09
LEWISTON ,NC 27849 DATE REPORTED 06/03/09
REVIEWED BY:
Rendering Analysis Method
PARAMETERS Date Analyst Code
COD, mg/l 5722 05/28/09 TRB HACH8000

-Environme Inc.- CHAIN OF CUSTODY RECORD I
P.O. Box 7085akmont Dr.
Greenville,NC 27858 Page ��I
Phone[phone]•Fax[phone] DISINFECTION CHLORINE NEUTRALIZED AT COLLECTION
CHLORINE
CLIENT:2 3 3 LZ pH CHECK(LAB)
UV
':�'e t t� l� u//yI S ❑ NONE CONTAINER TYPE,P/G
CHEMICAL PRESERVATION
A-NONE D-NAOH
U
z z Ld z cr B-HNO3 E-HCL
Fro m0 z cn
o w ~ w z ^ LU C-H,SO, F-ZINC ACETATE
COLLECTION ¢ o � o
t— 0 0 G-NATHIOSULFATE
SAMPLE LOCATION DATE TIME oP a LU
, a o a
•
CLASSIFICATION.
WASTEWATER(NPDES)
DRINKING WATER
DWQ/GW
SOLID WASTE SECTION
CHAIN OF CUSTODY MAINTAINED
DURING S ENT/DELIVERY
Y N
SAMPLES COLLECTED BY:
(Please Print)
�scre �.f•�/>1�
SAMPLES RECEIVED IN LAB AT oC
9ELINQU
SHED BY( PLER) DATEMME RECEIVED Y(SIG.) DATE/TIME COMMENTS:
SHED BY(SIG.) DATE/TIME REC E Y DA ERIME
-e - 0 (0: A i
RELIN UISHED BY(SIG.) DATE/TIME RECEIVED BY(SIG.) TE(fIME
PLEASE READ Instructions for completing this form on the reverse side. Sampler must place a"C"for composite sample or a"G"for N° 1 8 3 5 1 3
FORM#5 Grab sample in the blocks above for each parameter requested.

. a
SAMPLING INSTRUCTIONS AND FORM COMPLETION
FAILURE TO PROPERLY CHILL, CHEMICALLY PRESERVE, COLLECT IN PROPER BOTTLE
TYPES, MEET REQUIRED HOLDII*G TIMES, NEUTRALIZE CHLORINE IN CHLORINE
SENSITIVE SAMPLE,AND SEAL CO(ILERS WITH TAPE WILL RESULT IN SAMPLES BEING
REJECTED BY THIS LABORATORY AS PER NORTH CAROLINA REGULATORY CODE.
1) Samples not falling within the established guidelines will need to be re-collected. The client will be contacted and informed of the
deviation and asked to collect another set of samples. The client may wish for the laboratory to proceed with the analyses of the current
samples. Any samples analyzed outside of the required guidelines will be "qualified". This means that a note will be included on the
sample result and"Chain of Custody"specifying the deviation. The laboratory is also required to send a letter to the State noting the
deviations.
2)Sample Temperature.Samples for compliance monitoring must be chilled with wet ice to a temperature of 6C or less. Freezing is not
permitted.Samples delivered to the lab shortly after collection may not have had enough time to be chilled below 6C. In this case the
temperature at time of collection must be noted in the space provided.The samples will meet the requirements of the regulation if there
is a temperature drop from the time of collection until received in the lab. Regardless,all samples should be packed in wet ice using as
much ice as will fit in the cooler.
3) Sample Chemical Preservation. Many samples require a chemical preservation such as Sulfuric Acid or Sodium Hydroxide. The
laboratory will either provide the preservative in the sample bottle,or in the case of 40 mi. Volatiles Vials,provide a bottle of Acid with
detailed descriptions on how to collect the sample. Never rinse sample bottles before collecting samples. Any residue or liquid in the
bottle is required for proper chemical preservation.The lab must verify proper chemical preservation upon arrival in the lab and will note
this information in the spaces provided on the front of this form.
4)Chlorine Neutralization. Some samples require that any Total Chlorine Residual be removed at the time of collection. The lab will
provide the proper neutralizing agent in the sample bottle when technically possible.There are some samples (Total Kjeldahl Nitrogen
and Ammonia Nitrogen) where this is not possible due to interferences between the required chemical preservation(Acid) and the
dechlorinating agent.Therefore,these samples must be de-chlorinated at the time of collection before being placed in our sample bottles.
Sodium Thiosulfate is t he chemical of choice to neutralize chlorine. It must be added to your sample and them the sample checked for
Total Chlorine before the sample is poured in our bottle.Facilities using chlorine for disinfection should have a means of measuring Total
Chlorine.Non-chlorinated sample sources will not need to be checked.The person neutralizing the chorine must put his initials in the
"Chlorine Neutralized at Collection"row on the front of this form above the proper parameter. Samples such as Coliforms(which have
Thiosulfate in the bottles shipped from the lab) will be checked for proper neutralization upon arrival in the lab.It is also required that you
note the"Total Chlorine at Collection' on the front of this form for any sample locations applicable. This value would be before any
neutralization is performed.
5)A"C"for Composite Sample or a"G"for Grab Sample should be placed in the box for all requested parameters.
6)Other information required to be completed by the client are:
Collection Date and Collection Time for each sample location Temperature at Time of Collection
Printed name of person or persons collecting samples Signature,Date,and Time samples are relinquished
Other added sample locations and analyses required Type Of Disinfection
Deletion on the form for any samples which are not needed(example: dry upstream location)
Any other information felt to be pertinent should be included in the "Comments"section
CONSIDERATIONS:
Coliform and Enterococci samples have a holding time of 6 hours from time of collection to time of analysis.Therefore,samples should
be collected as late in the day as possible to allow enough time for transportation,checking in at the lab and analysis.
BOD samples have a 48 hour holding time and are set in the lab Monday through Friday.
Other samples such as Nitrate, Ortho Phosphorus, Settleable Matter, Turbidity,Color, and MBAS also have a 48 hour holding time. The
lab reserves the right to establish required sample collection and delivery dates in order to meet the required holding times.
CAUTION
These sample bottles may contain acid or other corrosive and potentially harmful chemicals. Laboratories are required to add these
chemicals for certain analyses in order to comply with EPA preservation requirements. Use extreme care when opening and handling
the bottles. If any chemical should get on your skin or clothes,flush liberally with water and seek medical attention.

Drinking Water ID: 37715
Wastewater ID: 10
P.O. BOX 7085, 114 OAKMONT DRIVE PHONE (252) /bb-b205
GREENVILLE, N.C. 27835-7085 FAX [phone]
ID#: 233 Y
PERDUE FARMS, INC. (LEWISTON)
MR. WAYNE BLACK
P.O. BOX 460 DATE COLLECTED: 05/27/09
LEWISTON ,NC 27849 DATE REPORTED : 06/03/09
REVIEWED BY:
Influent Analysis Method
PARAMETERS Date Analyst Code
COD, mg/1 2641 05/28/09 TRB HACH8000

Environ 1,1ne. CHAIN OF CUSTODY RECORD
P.O. Box 7U977TIt Oakmont Dr. I'a—C o
Greenville, NC 27858
Phone[phone]°Fax[phone] DISINFECTION
CHLORINE NEUTRALIZED AT COLLECTION
CHLORINE
CLIENT: 33 pH CHECK(LAB)
UV
1 n C ❑ NONE CONTAINER TYPE,P/G
CHEMICAL PRESERVATION
A-NONE D-NAOH
E
z � CO B-HNOa E-HCL
Fro Cr o z C/)
0 � 0 a LU C-H,SO4 F-ZINC ACETATE
= w 4� w z
COLLECTION Q o ww o oD Q G-NATHIOSULFATE
H U U U_
SAMPLE LOCATION DATE TIME Q Q o
CLASSIFICATION:
WASTEWATER(NPDES)
DRINKING WATER
DWQ/GW
SOLID WASTE SECTION
CHAIN OF CUSTODY MAINTAINED
DURING S MENT/DELIVERY
Y N
SAMPLES COLLECTED BY:
(Please Print)
SAMPLES RECEIVED IN LAB AT °C
RE UISHED BZ(SIGPLER) DATE/TIME RECEIVED Y(SIG.) DATEITIME COMMENTS:
ELINQUISHE Y(SIG.) DATE/TIME REC BY( ) D TE/TIME
6INQUISHED BY(SIG.) DATE/TIME RECEIVED BY(SIG.) ATE/11M
' PLEASE READ Instructions for completing this form on the reverse side. Sampler must place a"C"for composite sample or a°G for N 0— 1 8 3 5 0 3
FORM#5 Grab sample in the blocks above for each parameter requested.

{
SAMPLING INSTRUCTIONS AND FORM COMPLETION
FAILURE TO PROPERLY CHILL, CHEMICALLY PRESERVE, COLLECT IN PROPER BOTTLE
TYPES, MEET REQUIRED HOLDING TIMES, NEUTRALIZE CHLORINE IN CHLORINE
SENSITIVE SAMPLE,AND SEAL COERS WITH TAPE WILL RESULT IN SAMPLES BEING
REJECTED BY THIS LABORATORY 2 PER NORTH CAROLINA REGULATORY CODE.
1) Samples not falling within the established guidelines will need to be re-collected. The client will be contacted and informed of the
deviation and asked to collect another set of samples.The client may wish for the laboratory to proceed with the analyses of the current
samples. Any samples analyzed outside of the required guidelines will be "qualified". This means that a note will be included on the
sample result and"Chain of Custody"specifying the deviation. The laboratory is also required to send a letter to the State noting the
deviations.
2)Sample Temperature.Samples for compliance monitoring must be chilled with wet ice to a temperature of 6C or less.Freezing is not
permitted.Samples delivered to the lab shortly after collection may not have had enough time to be chilled below 6C. In this case the
temperature at time of collection must be noted in the space provided.The samples will meet the requirements of the regulation if there
is a temperature drop from the time of collection until received in the lab. Regardless,all samples should be packed in wet ice using as
much ice as will fit in the cooler.
3) Sample Chemical Preservation. Many samples require a chemical preservation such as Sulfuric Acid or Sodium Hydroxide. The
laboratory will either provide the preservative in the sample bottle,or in the case of 40 ml. Volatiles Vials,provide a bottle of Acid with
detailed descriptions on how to collect the sample. Never rinse sample bottles before collecting samples. Any residue or liquid in the
bottle is required for proper chemical preservation.The lab must verify proper chemical preservation upon arrival in the lab and will note
this information in the spaces provided on the front of this form.
4)Chlorine Neutralization. Some samples require that any Total Chlorine Residual be removed at the time of collection. The lab will
provide the proper neutralizing agent in the sample bottle when technically possible.There are some samples (Total Kjeldahl Nitrogen
and Ammonia Nitrogen) where this is not possible due to interferences between the required chemical preservation(Acid) and the
dechlorinating agent.Therefore,these samples must be de-chlorinated at the time of collection before being placed in our sample bottles.
Sodium Thiosulfate is t he chemical of choice to neutralize chlorine. It must be added to your sample and them the sample checked for
Total Chlorine before the sample is poured in our bottle.Facilities using chlorine for disinfection should have a means of measuring Total
Chlorine.Non-chlorinated sample sources will not need to be checked.The person neutralizing the chorine must put his initials in the
"Chlorine Neutralized at Collection"row on the front of this form above the proper parameter. Samples such as Coliforms(which have
Thiosulfate in the bottles shipped from the lab) will be checked for proper neutralization upon arrival in the lab.It is also required that you
note the"Total Chlorine at Collection' on the front of this form for any sample locations applicable. This value would be before any
neutralization is performed.
5)A"C"for Composite Sample or a"G"for Grab Sample should be placed in the box for all requested parameters.
6)Other information required to be completed by the client are:
Collection Date and Collection Time for each sample location Temperature at Time of Collection
Printed name of person or persons collecting samples Signature,Date,and Time samples are relinquished
Other added sample locations and analyses required Type Of Disinfection
Deletion on the form for any samples which are not needed(example: dry upstream location)
Any other information felt to be pertinent should be included in the "Comments"section
CONSIDERATIONS:
Coliform and Enterococci samples have a holding time of 6 hours from time of collection to time of analysis.Therefore,samples should
be collected as late in the day as possible to allow enough time for transportation,checking in at the lab and analysis.
BOD samples have a 48 hour holding time and are set in the lab Monday through Friday.
Other samples such as Nitrate,Ortho Phosphorus, Settleable Matter,Turbidity, Color,and MBAS also have a 48 hour holding time. The
lab reserves the right to establish required sample collection and delivery dates in order to meet the required holding times.
CAUTION
These sample bottles may contain acid or other corrosive and potentially harmful chemicals. Laboratories are required to add these
chemicals for certain analyses in order to comply with EPA preservation requirements. Use extreme care when opening and handling
the bottles. If any chemical should get on your skin or clothes,flush liberally with water and seek medical attention.

16704 Federal Register/Vol. 74, No. 68/Friday, April 10, 2009/Proposed Rules
TABLE HH-2 OF SUBPART HH-U.S. PER CAPITA WASTE DISPOSAL RATES-Continued
Waste per
Year capita ton/cap/ %to SWDS
yr
1974 ......................................................................................................................................................................... 0.71 100
1975 ......................................................................................................................................................................... 0.72 100
1976 ......................................................................................................................................................................... 0.73 100
1977 ......................................................................................................................................................................... 0.73 100
1978 ......................................................................................................................................................................... 0.74 100
1979 ......................................................................................................................................................................... 0.75 100
1980 ......................................................................................................................................................................... 0.75 100
1981 ......................................................................................................................................................................... 0.76 100
1982 ......................................................................................................................................................................... 0.77 100
1983 ......................................................................................................................................................................... 0.77 100
1984 ......................................................................................................................................................................... 0.78 100
1985 ......................................................................................................................................................................... 0.79 100
1986 ......................................................................................................................................................................... 0.79 100
1987 ......................................................................................................................................................................... 0.80 100
1988 ......................................................................................................................................................................... 0.80 100
1989 ......................................................................................................................................................................... 0.85 84
1990 ......................................................................................................................................................................... 0.84 77
1991 ......................................................................................................................................................................... 0.78 76
1992 ......................................................................................................................................................................... 0.76 72
1993 ......................................................................................................................................................................... 0.78 71
1994 ......................................................................................................................................................................... 0.77 67
1995 ......................................................................................................................................................................... 0.72 63
1996 ......................................................................................................................................................................... 0.71 62
1997 ......................................................................................................................................................................... 0.72 61
1998 ......................................................................................................................................................................... 0.78 61
1999 ......................................................................................................................................................................... 0.78 60
2000 ......................................................................................................................................................................... 0.84 61
2001 ......................................................................................................................................................................... 0.95 63
2002 ......................................................................................................................................................................... 1.06 66
2003 ......................................................................................................................................................................... 1.06 65
2004 ......................................................................................................................................................................... 1.06 64
2005 ......................................................................................................................................................................... 1.06 64
2006 ......................................................................................................................................................................... 1.06 64
Subpart 11-Wastewater Treatment §98.351 Reporting threshold. For flares,calculate the CO2 emissions
You must report GHG emissions only from pilot gas and other auxiliary
§98.350 Definition of source category. under this subpart if your facility fuels combusted in the flare,as
(a)A wastewater treatment system is contains a wastewater treatment process specified in subpart C of this part.Do
the collection of all processes that treat and the facility meets the requirements not include CO2 emissions resulting
or remove pollutants and contaminants, of either§98.2(a)(1)or(2). from the combustion of anaerobic
such as soluble organic matter, digester gas.
suspended solids,pathogenic §98.352 GHGs to report.
organisms,and chemicals from waters (a)You must report annual CH4 §98.353 Calculating GHG emissions.
released from industrial processes.This emissions from anaerobic wastewater (a)Estimate the annual CH4 mass
source category applies to on-site treatment processes. emissions from systems other than
wastewater treatment systems at pulp (b)You must report annual CO2 digesters using Equation II-1 of this
and paper mills,food processing plants, emissions from oil/water separators at section.The value of flow and COD
ethanol production plants, petroleum refineries. must be determined in accordance with
petrochemical facilities,and petroleum (c)You must report CO2,CH4,and the monitoring requirements specified
refining facilities. N20 emissions from the combustion of in§98.354.The flow and COD should
(b)This source category does not fuels in stationary combustion devices reflect the wastewater treated
include centralized domestic and fuels used in flares by following the anaerobically on site in anaerobic
wastewater treatment plants. requirements of subpart C of this part. systems such as lagoons.
12
CH4= [Flow„*COD*Bo*MCF*0.001] (Eq.II-1)
Where: Flow.=Volumetric flow rate of wastewater anaerobic treatment systems other than
CH4=Annual CH4 mass emissions from the sent to an anaerobic treatment system in digesters(kg/m3).
wastewater treatment system(metric month n(m3/month). Bo=Maximum CH4 producing potential of
tons). COD=Average monthly value for chemical wastewater(kg CH4/kg COD),default is
oxygen demand of wastewater entering 0.25.

16706 Federal Re iiter/Vol. 74, No. 68/Frida , Aril 10, 2009/Proposed Rules
g Y P
immediately following the missing data (e)Be. (o)Pressure at which flow is
incident. (f)MCF. measured(facilities with anaerobic
(b)If,for a particular parameter,no (g)Methane emissions. digesters).
quality-assured data are available prior (p)Destruction efficiency used
to the missing data incident,the (h)Type of oil/water separator (facilities with anaerobic digesters).
substitute data value shall be the first (Petroleum refineries). (q)Methane destruction(facilities
quality-assured value obtained after the (i)Emissions factor for the type of with anaerobic digesters).
missing data period. separator(petroleum refineries). (r)Fugitive methane(facilities with
§98.356 Data reporting requirements. (j)Carbon fraction in NMVOC anaerobic digesters).
(petroleum refineries).
In addition to the information (k)CO2 emissions(petroleum §98.357 Records that must be retained.
required by§98.3(c),each annual report refineries). In addition to the information
must contain the following information (1)Total volumetric flow of digester required by§98.3(g),you must retain
for the wastewater treatment system. the calibration records for all
gas(facilities with anaerobic digesters).
(a)Type of wastewater treatment monitoring equipment.
system. (m)CH4 concentration of digester gas
(b)Percent of wastewater treated at (facilities with anaerobic digesters). §98.358 Definitions.
each system component. (n)Temperature at which flow is All terms used in this subpart have
(c)COD. measured(facilities with anaerobic the same meaning given in the Clean Air
(d)Influent flow rate. digesters). Act and subpart A of this part.
TABLE II-1 OF SUBPART II—EMISSION FACTORS
Factors Default Units
value
Bo ................................................................................................... 0.2 kg COD.
MCF—anaerobic deep lagoon, anaerobic reactor (e.g., upflow L�_0.8 Fraction-
anaerobic sludge blanket,fixed film).
MCF—anaerobic shallow lagoon(less than 2 m) ........................ 0.2 Fraction.
MCF—centralized aerobic treatment system,well managed ....... 0 Fraction.
MCF—Centralized aerobic treatment system, not well managed 0.3 Fraction.
(overloaded).
Anaerobic digester for sludge ....................................................... 0.8 Fraction.
C fraction in NMOC ....................................................................... 0.6 Fraction.
EF sep—Gravity Type(Uncovered) .............................................. 1.11E-01 Kg NMVOC/m3 wastewater
EF sep—Gravity Type(Covered) ................................................. 3.30E-03 Kg NMVOC/m3 wastewater.
EF sep—Gravity Type—(Covered and Connected to a Destruc- 0 Kg NMVOC/m3 wastewater.
tion Device).
DAF or IAF—uncovered................................................................ 4.00E-34 Kg NMVOC/m3 wastewater.
DAF or IAF—covered.................................................................... 1.20E-44 Kg NMVOC/m3 wastewater.
DAF or IAF—covered and connected to a destruction device ..... 0 Kg NMVOC/m3 wastewater.
DAF=dissolved air flotation type.
IAF=induced air flotation type.
Subpart JJ—Manure Management spread or pasture/range/paddock and turkey production on litter,and
systems. deep bedding systems for cattle and
§98.360 Definition of the source category. swine.
(a)This source category consists of §98.361 Reporting threshold.
manure management systems for You must report GHG emissions
(6)Manure composting.
g Y P
livestock manure. under this subpart if your facility (b)You must re ort CO2,CH4,and
(b)A manure management system is contains a manure management system N20 emissions from the combustion of
as a system that stabilizes or stores and the facility meets the requirements supplemental fuels used in flares by
livestock manure in one or more of the of either§98.2(a)(1)or(2). following the requirements of subpart C
following system components: of this part.For flares,calculate the CO2
uncovered anaerobic lagoons,liquid/ §98.362 GIiGs to report. emissions only from pilot gas and other
slurry systems,storage pits,digesters, (a)You must report annual aggregate auxiliary fuels combusted in the flare,as
drylots,solid manure storage,feedlots CH4 and N20 emissions for each of the specified in subpart C of this part.Do
and other dry lots,high rise houses for following manure management system not include CO2 emissions resulting
poultry production(poultry without (MMS)components at the facility: from the combustion of digester gas in
litter),poultry production with litter, (1)Liquid/slurry systems such as flares.
deep bedding systems for cattle and tanks and ponds.
swine,and manure composting.This (2)Storage pits. (c)A facility that is subject to this rule
definition of manure management (3)Uncovered anaerobic lagoons used only because of emissions from manure
system encompasses the treatment of for stabilization or storage or both. management systems is not required to
wastewaters from manure. (4)Digesters,including covered report emissions from fuels used in
(c)This source category does not anaerobic lagoons. stationary combustion devices other
include components at a livestock (5)Solid manure storage including than flares.
operation unrelated to the stabilization feedlots and other dry lots,high rise
or storage of manure such as daily houses for caged laying hens,broiler