Name:

Title:

Company:

Sign Date:

Name:

Title:

Company:

Sign Date:

Permitted Facility Representative / Date Testing Company Representative / Date

Northport Unit 3 ICR Test Program

Final Test Report 

for

/ /

Based on information and belief formed 

after reasonable inquiry, I certify that the 

statements and information in this test 

report are true, accurate, and complete.

I have reviewed all testing details and 

results in this test report and hereby 

certify that the test report is authentic 

and accurate.

Monday, February 28, 2011 Page 1 of 52
Northport Unit 3 ICR Test Program

Facility Information:

Northport

301 Eatons Neck Road

Northport NY 11768

Contact: Paul Lynch

Phone: 516-545-2564

Fax: 516-545-2582

Email: paul.lynch@us.ngrid.com

Testing Company:

AirNova Inc.

5845 Clayton Avenue

Pennsauken NJ 08109

Contact:Lenny D. Katerynczuk

Phone: 856-486-1500

Fax: 856-486-9896

Email: lenny@airnova.com

Air Permit Number:

1-4726-00130/00041

Permitted Source ID/Name:

U-00003 Boiler 3

Permitted Maximum Process Rate:

N/A

Max. Normal Operation Process Rate:

N/A

Target Process Test Rate

N/A

Description of the source (including control equipment). Please see the attachments for source or

 process flow diagram:

This source is a tangential fired external combustion boiler used for electric generation. Rated at 385 MW and can 

fire either #6 residual oil or natural gas. Exhaust gases from the boiler are split between two air heaters then travel 

through individual dual pass Buell electrostatic precipitators. From the ESP exhaust gas is passed through dual 

induced draft fans then enters the stack through dual breechings.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: Enter ARS ID FRS #: Enter FRS ID

SCC / Description 10100404 External Combustion Boilers - Electric Generation - Residual Oil - Grade 6 Oil: 

Tangential Firing 

The following state and federal regulations that apply to the proposed testing:

Location

Round

Duct

Diam.

Distance from 

upstream dist.

Distance from

downstream dist.

Number of

Traverse Ports

Equiv. 

Diam

Min.Travers 

Points

Rect. Duct 

Length /Width

Duct near 

stack 

breaching

0 108 124 65.29 12 12 4 24

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Duct near % H2O Method 1 - 4 3 180 0

stack 

breaching

Regulation Description Compound Limit Unit

0

Monday, February 28, 2011 Page 2 of 52
Northport Unit 3 ICR Test Program

Duct near Carbon Monoxide Method 10 3 120 0

stack 

breaching

Duct near Formaldehyde Method 0011 3 120 0

stack 

breaching

Duct near 2,3,7,8-TCDD Method 23 3 480 0

stack 

breaching

Duct near 1,2,3,7,8-PeCDD Method 23 3 480 0

stack 

breaching

Duct near OCDD Method 23 3 480 0

stack 

breaching

Duct near 2,3,7,8-TCDF Method 23 3 480 0

stack 

breaching

Duct near 1,2,3,7,8-PeCDF Method 23 3 480 0

stack 

breaching

Duct near 2,3,4,7,8-PeCDF Method 23 3 480 0

stack 

breaching

Duct near 1,2,3,4,6,7,8-HpCDF Method 23 3 480 0

stack 

breaching

Duct near OCDF Method 23 3 480 0

stack 

breaching

Duct near Other TCDD Method 23 3 480 0

stack 

breaching

Duct near Other PeCDD Method 23 3 480 0

stack 

breaching

Duct near Other HxCDD Method 23 3 480 0

stack 

breaching

Duct near Other HpCDD Method 23 3 480 0

stack 

breaching

Duct near Other TCDF Method 23 3 480 0

stack 

breaching

Duct near Other PeCDF Method 23 3 480 0

stack 

breaching

Duct near Other HxCDF Method 23 3 480 0

stack 

breaching

Duct near Other HpCDF Method 23 3 480 0

stack 

breaching

Duct near 3,3',4,4'-TCB (PCB77) Method 23 3 480 0

stack 

breaching

Monday, February 28, 2011 Page 3 of 52
Northport Unit 3 ICR Test Program

Duct near 3,4,4',5-TCB (PCB81) Method 23 3 480 0

stack 

breaching

Duct near 2,3,3',4,4'-PeCB (PCB105) Method 23 3 480 0

stack 

breaching

Duct near 2,3,4,4',5-PeCB (PCB114) Method 23 3 480 0

stack 

breaching

Duct near 2,3',4,4',5-PeCB (PCB118) Method 23 3 480 0

stack 

breaching

Duct near 2',3,4,4',5-PeCB (PCB123) Method 23 3 480 0

stack 

breaching

Duct near 3,3',4,4',5-PeCB (PCB126) Method 23 3 480 0

stack 

breaching

2,3,3',4,4',5/2,3,3',4,4',5'-

HxCB (PCBs156/157)

Duct near Method 23 3 480 0

stack 

breaching

Duct near 2,3',4,4',5,5'-HxCB (PCB167) Method 23 3 480 0

stack 

breaching

Duct near 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 480 0

stack 

breaching

2,3,3',4,4',5,5'-HpCB 

(PCB189)

Duct near Method 23 3 480 0

stack 

breaching

Total organic compounds 

(TOC) as Propane

Duct near Method 25A 3 120 0

stack 

breaching

Duct near Hydrogen Fluoride Method 26A 3 180 0

stack 

breaching

Duct near Hydrogen Chloride Method 26A 3 180 0

stack 

breaching

Duct near Hydrogen Chloride Method 26 3 180 0

stack 

breaching

Duct near Hydrogen Fluoride Method 26 3 180 0

stack 

breaching

Duct near Filterable PM2.5 OTM - 27/28 3 364 0

stack 

breaching

Inorganic (Aqueous) 

Condensible Part.

Duct near OTM - 27/28 3 364 0

stack 

breaching

Organic Condensible 

Particulate

Duct near OTM - 27/28 3 364 0

stack 

breaching

Duct near Total PM2.5 OTM - 27/28 3 364 0

stack 

breaching

Monday, February 28, 2011 Page 4 of 52
Northport Unit 3 ICR Test Program

The following describes any modifications and/or deviations to the applicable test 

methods. If alternative methods were requested, see the attachments for documentation 

of request AND approval, including dates.

Duct near Filterable Particulate Method 29 3 240 0

stack 

breaching

Duct near Antimony Method 29 3 240 0

stack 

breaching

Duct near Manganese Method 29 3 240 0

stack 

breaching

Duct near Cadmium Method 29 3 240 0

stack 

breaching

Duct near Selenium Method 29 3 240 0

stack 

breaching

Duct near Lead Method 29 3 240 0

stack 

breaching

Duct near Chromium Method 29 3 240 0

stack 

breaching

Duct near Arsenic Method 29 3 240 0

stack 

breaching

Duct near Beryllium Method 29 3 240 0

stack 

breaching

Duct near Nickel Method 29 3 240 0

stack 

breaching

Duct near O2 Method 3A O2 3 480 0

stack 

breaching

Duct near Co2 Method 3A CO2 3 480 0

stack 

breaching

Duct near O2 Method 3A O2 3 120 0

stack 

breaching

Duct near Co2 Method 3A CO2 3 120 0

stack 

breaching

Duct near O2 Method 3A O2 3 240 0

stack 

breaching

Duct near Co2 Method 3A CO2 3 240 0

stack 

breaching

Duct near Filterable Particulate Method 5 3 240 0

stack 

breaching

Duct near Sulfur Dioxide Method 6C 3 180 0

stack 

breaching

Duct near Nitrogen oxides (NOx) Method 7E 3 180 0

stack 

breaching

Monday, February 28, 2011 Page 5 of 52
Northport Unit 3 ICR Test Program

The following describes any modifications and/or deviations to the applicable test 

methods. If alternative methods were requested, see the attachments for documentation 

of request AND approval, including dates.

Selection of sampling location is not in accordance with applicable methods. 3D traverses were conducted in 

accordance with a plan previously approved by Bill Maxwell to verify cyclonic conditions were not present in the 

sampling location utilized during testing.

Monday, February 28, 2011 Page 6 of 52
Northport Unit 3 ICR Test Program

Sampling / Stack Data Results Summary

Location Duct near stack breaching - Method 0011

Average

Run Number NPT3 R1N NPT3 R1S NPT3 R2N

Test Date 6/12/2010 6/19/2010 6/19/2010

Run Start Time 6/19/2010 

8:05:00 AM

6/19/2010 

8:05:00 

AM

6/19/2010 

11:30:00 AM

Run Finish Time 6/19/2010 

10:29:00 AM

6/19/2010 

10:29:00 

AM

6/19/2010 

1:56:00 PM

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 90.181 100.238 88.754 93.058

Moisture Content of Stack Gas, % 7.72 8.24 7.84 7.933

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Carbon Dioxide, % 10.7 10.8 10 10.500

Oxygen, % 7.7 7.6 8.5 7.933

Average Stack Gas Temperature, °F 289.42 303.46 292.58 295.153

Dry Volumetric Flow Rate, dry scfm 344,252.5 392,502.9 350,318.1 362,357.833

Actual Wet Volumetric Flue Gas Flow Rate, acfm 525,803.4 614,804.4 538,023.6 559,543.800

Percent Isokinetic of Sampling Rate, % 95.9 93.5 92.8 94.067

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 28, 2011 Page 7 of 52
Northport Unit 3 ICR Test Program

Location Duct near stack breaching - Method 0011 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Location Duct near stack breaching - Method 10

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Monday, February 28, 2011 Page 8 of 52
Northport Unit 3 ICR Test Program

Location Duct near stack breaching - Method 10 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Duct near stack breaching - Method 23

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Monday, February 28, 2011 Page 9 of 52
Northport Unit 3 ICR Test Program

Location Duct near stack breaching - Method 23 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Location Duct near stack breaching - Method 25A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Monday, February 28, 2011 Page 10 of 52
Northport Unit 3 ICR Test Program

Location Duct near stack breaching - Method 25A 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Duct near stack breaching - Method 26A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Monday, February 28, 2011 Page 11 of 52
Northport Unit 3 ICR Test Program

Location Duct near stack breaching - Method 26A 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Location Duct near stack breaching - Method 29 

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Monday, February 28, 2011 Page 12 of 52
Northport Unit 3 ICR Test Program

Location Duct near stack breaching - Method 29 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Location Duct near stack breaching - Method 6C

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Monday, February 28, 2011 Page 13 of 52
Northport Unit 3 ICR Test Program

Location Duct near stack breaching - Method 6C 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Duct near stack breaching - Method 7E

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Monday, February 28, 2011 Page 14 of 52
Northport Unit 3 ICR Test Program

Location Duct near stack breaching - Method 7E 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Duct near stack breaching - OTM - 27/28

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Monday, February 28, 2011 Page 15 of 52
Northport Unit 3 ICR Test Program

Location Duct near stack breaching - OTM - 27/28 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Monday, February 28, 2011 Page 16 of 52
Northport Unit 3 ICR Test Program

Emissions Summary

Location: Duct near stack breaching - Method 0011

Compound: Formaldehyde

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.0069 0.00645 0.00635 0.007

lb/mmBtuO2 2.45E-06 2.05E-06 2.44E-06 0.000

ppm 2.16E-03 1.82E-03 2.02E-03 0.002

ppm@7%O2 2.27E-03 1.90E-03 2.26E-03 0.002

Location: Duct near stack breaching - Method 0011 3

Compound: Formaldehyde

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.00635 0.00638 0.006 0.006

lb/mmBtuO2 2.14E-06 2.40E-06 2.17E-06 0.000

ppm 1.80E-03 1.97E-03 1.79E-03 0.002

ppm@7%O2 1.99E-03 2.23E-03 2.02E-03 0.002

Location: Duct near stack breaching - Method 10

Compound: Carbon Monoxide

Average

Run NPT3 R1N NPT3 R1S NPT3 R2N

Elb/hr 2.01E+01 2.51E+01 1.15E+01 18.900

lb/mmBtuO2 1.53E-02 2.01E-02 8.64E-03 0.015

mg/dscm 1.54E+01 1.98E+01 8.72E+00 14.640

Location: Duct near stack breaching - Method 10 3

Compound: Carbon Monoxide

Average

Run NPT3 R2S NPT3 R3N NPT3 R3S

Elb/hr 2.15E+01 1.56E+01 2.41E+01 20.400

lb/mmBtuO2 1.37E-02 1.08E-02 1.57E-02 0.013

mg/dscm 1.56E+01 1.21E+01 1.77E+01 15.133

Location: Duct near stack breaching - Method 23

Compound: 1,2,3,4,6,7,8-HpCDF

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.00000001832 0.000000003765 0.000000012319 0.000

lb/mmBtuO2 2.05E-12 4.37E-13 1.32E-12 0.000

ng/dscm 2.06E-03 4.31E-04 1.33E-03 0.001

ng/dscm@7%O2 2.39E-03 5.08E-04 1.53E-03 0.001

Compound: 1,2,3,7,8-PeCDD

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.00000000214 0.00000000152 0.00000000132 0.000

lb/mmBtuO2 2.40E-13 1.77E-13 1.41E-13 0.000

ng/dscm 2.40E-04 1.74E-04 1.43E-04 0.000

Monday, February 28, 2011 Page 17 of 52
Northport Unit 3 ICR Test Program

ng/dscm@7%O2 2.78E-04 2.05E-04 1.64E-04 0.000

Compound: 1,2,3,7,8-PeCDF

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.00000000663 0.000000000795 0.00000000295 0.000

lb/mmBtuO2 7.44E-13 9.24E-14 3.16E-13 0.000

ng/dscm 7.44E-04 9.09E-05 3.18E-04 0.000

ng/dscm@7%O2 8.62E-04 1.07E-04 3.65E-04 0.000

Compound: 2,3,3',4,4',5,5'-HpCB (PCB189)

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.0000000279 0.00000000501 0.0000000147 0.000

lb/mmBtuO2 3.13E-12 5.82E-13 1.57E-12 0.000

ng/dscm 3.13E-03 5.73E-04 1.59E-03 0.002

ng/dscm@7%O2 3.63E-03 6.75E-04 1.83E-03 0.002

Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.00000065 0.0000001266 0.000000316 0.000

lb/mmBtuO2 7.29E-11 1.47E-11 3.38E-11 0.000

ng/dscm 7.30E-02 1.45E-02 3.41E-02 0.041

ng/dscm@7%O2 8.46E-02 1.71E-02 3.92E-02 0.047

Compound: 2,3,3',4,4'-PeCB (PCB105)

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.00000209 0.000000489 0.00000119 0.000

lb/mmBtuO2 2.34E-10 5.68E-11 1.27E-10 0.000

ng/dscm 2.35E-01 5.59E-02 1.28E-01 0.140

ng/dscm@7%O2 2.72E-01 6.58E-02 1.47E-01 0.162

Compound: 2,3',4,4',5,5'-HxCB (PCB167)

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.000000212 0.0000000431 0.000000105 0.000

lb/mmBtuO2 2.38E-11 5.01E-12 1.12E-11 0.000

ng/dscm 2.38E-02 4.93E-03 1.13E-02 0.013

ng/dscm@7%O2 2.76E-02 5.81E-03 1.30E-02 0.015

Compound: 2,3,4,4',5-PeCB (PCB114)

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.000000164 0.000000036 0.0000000919 0.000

lb/mmBtuO2 1.84E-11 4.18E-12 9.83E-12 0.000

ng/dscm 1.84E-02 4.12E-03 9.92E-03 0.011

ng/dscm@7%O2 2.13E-02 4.85E-03 1.14E-02 0.013

Compound: 2,3',4,4',5-PeCB (PCB118)

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.00000543 0.00000143 0.0000031 0.000

Monday, February 28, 2011 Page 18 of 52
Northport Unit 3 ICR Test Program

lb/mmBtuO2 6.09E-10 1.66E-10 3.32E-10 0.000

ng/dscm 6.10E-01 1.64E-01 3.35E-01 0.370

ng/dscm@7%O2 7.07E-01 1.93E-01 3.85E-01 0.428

Compound: 2',3,4,4',5-PeCB (PCB123)

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.000000237 0.0000000239 0.0000000697 0.000

lb/mmBtuO2 2.66E-11 2.78E-12 7.46E-12 0.000

ng/dscm 2.66E-02 2.73E-03 7.53E-03 0.012

ng/dscm@7%O2 3.08E-02 3.22E-03 8.65E-03 0.014

Compound: 2,3,4,7,8-PeCDF

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.00000000562 0.000000000828 0.00000000416 0.000

lb/mmBtuO2 6.30E-13 9.62E-14 4.45E-13 0.000

ng/dscm 6.31E-04 9.47E-05 4.49E-04 0.000

ng/dscm@7%O2 7.31E-04 1.12E-04 5.16E-04 0.000

Compound: 2,3,7,8-TCDD

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.00000000148 0.000000000917 0.00000000096 0.000

lb/mmBtuO2 1.66E-13 1.07E-13 1.03E-13 0.000

ng/dscm 1.66E-04 1.05E-04 1.04E-04 0.000

ng/dscm@7%O2 1.92E-04 1.24E-04 1.19E-04 0.000

Compound: 2,3,7,8-TCDF

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.00000000479 0.000000000831 0.00000000149 0.000

lb/mmBtuO2 5.37E-13 9.66E-14 1.59E-13 0.000

ng/dscm 5.38E-04 9.50E-05 1.61E-04 0.000

ng/dscm@7%O2 6.23E-04 1.12E-04 1.85E-04 0.000

Compound: 3,3',4,4',5,5'-HxCB (PCB169)

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.00000000581 0.0000000026 0.00000000355 0.000

lb/mmBtuO2 6.52E-13 3.02E-13 3.80E-13 0.000

ng/dscm 6.52E-04 2.97E-04 3.83E-04 0.000

ng/dscm@7%O2 7.55E-04 3.50E-04 4.40E-04 0.001

Compound: 3,3',4,4',5-PeCB (PCB126)

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.000000033 0.00000000468 0.0000000124 0.000

lb/mmBtuO2 3.70E-12 5.44E-13 1.33E-12 0.000

ng/dscm 3.70E-03 5.35E-04 1.34E-03 0.002

ng/dscm@7%O2 4.29E-03 6.30E-04 1.54E-03 0.002

Compound: 3,3',4,4'-TCB (PCB77)

Average

Monday, February 28, 2011 Page 19 of 52
Northport Unit 3 ICR Test Program

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.000000515 0.0000000355 0.000000173 0.000

lb/mmBtuO2 5.78E-11 4.12E-12 1.85E-11 0.000

ng/dscm 5.78E-02 4.06E-03 1.87E-02 0.027

ng/dscm@7%O2 6.70E-02 4.78E-03 2.15E-02 0.031

Compound: 3,4,4',5-TCB (PCB81)

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.0000000325 0.00000000755 0.0000000165 0.000

lb/mmBtuO2 3.65E-12 8.77E-13 1.77E-12 0.000

ng/dscm 3.65E-03 8.63E-04 1.78E-03 0.002

ng/dscm@7%O2 4.23E-03 1.02E-03 2.04E-03 0.002

Compound: OCDD

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.0000000496 0.000000037 0.0000000336 0.000

lb/mmBtuO2 5.56E-12 4.30E-12 3.59E-12 0.000

ng/dscm 5.57E-03 4.23E-03 3.63E-03 0.004

ng/dscm@7%O2 6.45E-03 4.98E-03 4.17E-03 0.005

Compound: OCDF

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.0000000227 0.00000000869 0.0000000121 0.000

lb/mmBtuO2 2.55E-12 1.01E-12 1.29E-12 0.000

ng/dscm 2.55E-03 9.94E-04 1.31E-03 0.002

ng/dscm@7%O2 2.95E-03 1.17E-03 1.50E-03 0.002

Compound: Other HpCDD

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.000000012 0.00000000376 0 0.000

lb/mmBtuO2 1.35E-12 4.37E-13 0.00E+00 0.000

ng/dscm 1.35E-03 4.30E-04 0.00E+00 0.001

ng/dscm@7%O2 1.56E-03 5.07E-04 0.00E+00 0.001

Compound: Other HpCDF

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0 0 0 0.000

lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Other HxCDD

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.0000000123 0 0 0.000

lb/mmBtuO2 1.38E-12 0.00E+00 0.00E+00 0.000

ng/dscm 1.38E-03 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 1.60E-03 0.00E+00 0.00E+00 0.001

Monday, February 28, 2011 Page 20 of 52
Northport Unit 3 ICR Test Program

Compound: Other HxCDF

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.0000000283 0.00000000111 0 0.000

lb/mmBtuO2 3.17E-12 1.29E-13 0.00E+00 0.000

ng/dscm 3.18E-03 1.27E-04 0.00E+00 0.001

ng/dscm@7%O2 3.68E-03 1.50E-04 0.00E+00 0.001

Compound: Other PeCDD

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.0000000101 0 0 0.000

lb/mmBtuO2 1.13E-12 0.00E+00 0.00E+00 0.000

ng/dscm 1.13E-03 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 1.31E-03 0.00E+00 0.00E+00 0.000

Compound: Other PeCDF

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.0000000603 0.00000000227 0 0.000

lb/mmBtuO2 6.76E-12 2.64E-13 0.00E+00 0.000

ng/dscm 6.77E-03 2.60E-04 0.00E+00 0.002

ng/dscm@7%O2 7.84E-03 3.06E-04 0.00E+00 0.003

Compound: Other TCDD

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.0000000375 0.00000000822 0 0.000

lb/mmBtuO2 4.21E-12 9.55E-13 0.00E+00 0.000

ng/dscm 4.21E-03 9.40E-04 0.00E+00 0.002

ng/dscm@7%O2 4.88E-03 1.11E-03 0.00E+00 0.002

Compound: Other TCDF

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.000000156 0.00000000166 0 0.000

lb/mmBtuO2 1.75E-11 1.93E-13 0.00E+00 0.000

ng/dscm 1.75E-02 1.90E-04 0.00E+00 0.006

ng/dscm@7%O2 2.03E-02 2.24E-04 0.00E+00 0.007

Location: Duct near stack breaching - Method 23 3

Compound: 1,2,3,4,6,7,8-HpCDF

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.000000008441 0.00000001788 0.0000000072 0.000

lb/mmBtuO2 7.85E-13 1.63E-12 6.88E-13 0.000

ng/dscm 8.90E-04 1.82E-03 7.74E-04 0.001

ng/dscm@7%O2 9.10E-04 1.89E-03 7.97E-04 0.001

Compound: 1,2,3,7,8-PeCDD

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.00000000124 0.00000000166 0.00000000212 0.000

Monday, February 28, 2011 Page 21 of 52
Northport Unit 3 ICR Test Program

lb/mmBtuO2 1.15E-13 1.51E-13 2.02E-13 0.000

ng/dscm 1.31E-04 1.69E-04 2.28E-04 0.000

ng/dscm@7%O2 1.34E-04 1.75E-04 2.35E-04 0.000

Compound: 1,2,3,7,8-PeCDF

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.00000000213 0.00000000432 0.00000000442 0.000

lb/mmBtuO2 1.98E-13 3.94E-13 4.22E-13 0.000

ng/dscm 2.25E-04 4.40E-04 4.75E-04 0.000

ng/dscm@7%O2 2.30E-04 4.56E-04 4.89E-04 0.000

Compound: 2,3,3',4,4',5,5'-HpCB (PCB189)

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.0000000175 0.0000000159 0.0000000178 0.000

lb/mmBtuO2 1.63E-12 1.45E-12 1.70E-12 0.000

ng/dscm 1.85E-03 1.62E-03 1.91E-03 0.002

ng/dscm@7%O2 1.89E-03 1.68E-03 1.97E-03 0.002

Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.0000003756 0.0000003177 0.0000004034 0.000

lb/mmBtuO2 3.49E-11 2.90E-11 3.85E-11 0.000

ng/dscm 3.96E-02 3.24E-02 4.34E-02 0.038

ng/dscm@7%O2 4.05E-02 3.36E-02 4.47E-02 0.040

Compound: 2,3,3',4,4'-PeCB (PCB105)

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.00000129 0.00000141 0.00000141 0.000

lb/mmBtuO2 1.20E-10 1.29E-10 1.35E-10 0.000

ng/dscm 1.36E-01 1.44E-01 1.52E-01 0.144

ng/dscm@7%O2 1.39E-01 1.49E-01 1.57E-01 0.148

Compound: 2,3',4,4',5,5'-HxCB (PCB167)

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.000000126 0.000000107 0.000000131 0.000

lb/mmBtuO2 1.17E-11 9.76E-12 1.25E-11 0.000

ng/dscm 1.33E-02 1.09E-02 1.41E-02 0.013

ng/dscm@7%O2 1.36E-02 1.13E-02 1.45E-02 0.013

Compound: 2,3,4,4',5-PeCB (PCB114)

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.0000000988 0.000000104 0.0000000948 0.000

lb/mmBtuO2 9.19E-12 9.48E-12 9.05E-12 0.000

ng/dscm 1.04E-02 1.06E-02 1.02E-02 0.010

ng/dscm@7%O2 1.06E-02 1.10E-02 1.05E-02 0.011

Compound: 2,3',4,4',5-PeCB (PCB118)

Average

Monday, February 28, 2011 Page 22 of 52
Northport Unit 3 ICR Test Program

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.00000381 0.0000034 0.00000371 0.000

lb/mmBtuO2 3.54E-10 3.10E-10 3.54E-10 0.000

ng/dscm 4.02E-01 3.47E-01 3.99E-01 0.383

ng/dscm@7%O2 4.11E-01 3.60E-01 4.11E-01 0.394

Compound: 2',3,4,4',5-PeCB (PCB123)

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.0000000666 0.000000101 0.000000117 0.000

lb/mmBtuO2 6.19E-12 9.21E-12 1.12E-11 0.000

ng/dscm 7.02E-03 1.03E-02 1.26E-02 0.010

ng/dscm@7%O2 7.17E-03 1.07E-02 1.30E-02 0.010

Compound: 2,3,4,7,8-PeCDF

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.00000000131 0.00000000336 0.00000000182 0.000

lb/mmBtuO2 1.22E-13 3.06E-13 1.74E-13 0.000

ng/dscm 1.38E-04 3.43E-04 1.96E-04 0.000

ng/dscm@7%O2 1.41E-04 3.56E-04 2.02E-04 0.000

Compound: 2,3,7,8-TCDD

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.00000000107 0.00000000118 0.00000000137 0.000

lb/mmBtuO2 9.95E-14 1.08E-13 1.31E-13 0.000

ng/dscm 1.13E-04 1.20E-04 1.47E-04 0.000

ng/dscm@7%O2 1.15E-04 1.24E-04 1.51E-04 0.000

Compound: 2,3,7,8-TCDF

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.00000000106 0.00000000228 0.00000000281 0.000

lb/mmBtuO2 9.85E-14 2.08E-13 2.68E-13 0.000

ng/dscm 1.12E-04 2.32E-04 3.02E-04 0.000

ng/dscm@7%O2 1.14E-04 2.41E-04 3.11E-04 0.000

Compound: 3,3',4,4',5,5'-HxCB (PCB169)

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.00000000304 0.00000000485 0.00000000523 0.000

lb/mmBtuO2 2.83E-13 4.42E-13 5.00E-13 0.000

ng/dscm 3.21E-04 4.94E-04 5.62E-04 0.000

ng/dscm@7%O2 3.28E-04 5.12E-04 5.79E-04 0.000

Compound: 3,3',4,4',5-PeCB (PCB126)

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.00000000682 0.0000000162 0.0000000229 0.000

lb/mmBtuO2 6.34E-13 1.48E-12 2.19E-12 0.000

ng/dscm 7.19E-04 1.65E-03 2.46E-03 0.002

ng/dscm@7%O2 7.35E-04 1.71E-03 2.53E-03 0.002

Monday, February 28, 2011 Page 23 of 52
Northport Unit 3 ICR Test Program

Compound: 3,3',4,4'-TCB (PCB77)

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.0000000708 0.000000262 0.000000351 0.000

lb/mmBtuO2 6.58E-12 2.39E-11 3.35E-11 0.000

ng/dscm 7.47E-03 2.67E-02 3.78E-02 0.024

ng/dscm@7%O2 7.63E-03 2.77E-02 3.89E-02 0.025

Compound: 3,4,4',5-TCB (PCB81)

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.0000000113 0.0000000243 0.0000000191 0.000

lb/mmBtuO2 1.05E-12 2.22E-12 1.82E-12 0.000

ng/dscm 1.19E-03 2.48E-03 2.05E-03 0.002

ng/dscm@7%O2 1.22E-03 2.57E-03 2.11E-03 0.002

Compound: OCDD

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.0000000459 0.0000000263 0.0000000506 0.000

lb/mmBtuO2 4.27E-12 2.40E-12 4.83E-12 0.000

ng/dscm 4.84E-03 2.68E-03 5.44E-03 0.004

ng/dscm@7%O2 4.95E-03 2.78E-03 5.60E-03 0.004

Compound: OCDF

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.0000000108 0.00000000796 0.0000000115 0.000

lb/mmBtuO2 1.00E-12 7.26E-13 1.10E-12 0.000

ng/dscm 1.14E-03 8.11E-04 1.24E-03 0.001

ng/dscm@7%O2 1.17E-03 8.41E-04 1.28E-03 0.001

Compound: Other HpCDD

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.00000000531 0.00000000802 0.00000000832 0.000

lb/mmBtuO2 4.94E-13 7.31E-13 7.95E-13 0.000

ng/dscm 5.60E-04 8.18E-04 8.95E-04 0.001

ng/dscm@7%O2 5.72E-04 8.49E-04 9.22E-04 0.001

Compound: Other HpCDF

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.00000000523 0 0 0.000

lb/mmBtuO2 4.86E-13 0.00E+00 0.00E+00 0.000

ng/dscm 5.52E-04 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 5.64E-04 0.00E+00 0.00E+00 0.000

Compound: Other HxCDD

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0 0.00000000636 0.00000000718 0.000

lb/mmBtuO2 0.00E+00 5.80E-13 6.86E-13 0.000

Monday, February 28, 2011 Page 24 of 52
Northport Unit 3 ICR Test Program

ng/dscm 0.00E+00 6.48E-04 7.72E-04 0.000

ng/dscm@7%O2 0.00E+00 6.72E-04 7.95E-04 0.000

Compound: Other HxCDF

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.00000000962 0.0000000214 0.00000000996 0.000

lb/mmBtuO2 8.94E-13 1.95E-12 9.51E-13 0.000

ng/dscm 1.01E-03 2.18E-03 1.07E-03 0.001

ng/dscm@7%O2 1.03E-03 2.26E-03 1.10E-03 0.001

Compound: Other PeCDD

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0 0.0000000032 0.0000000064 0.000

lb/mmBtuO2 0.00E+00 2.92E-13 6.11E-13 0.000

ng/dscm 0.00E+00 3.26E-04 6.88E-04 0.000

ng/dscm@7%O2 0.00E+00 3.38E-04 7.08E-04 0.000

Compound: Other PeCDF

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.000000013 0.0000000492 0.0000000233 0.000

lb/mmBtuO2 1.21E-12 4.49E-12 2.23E-12 0.000

ng/dscm 1.37E-03 5.02E-03 2.51E-03 0.003

ng/dscm@7%O2 1.40E-03 5.21E-03 2.58E-03 0.003

Compound: Other TCDD

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.00000000809 0.0000000149 0.0000000175 0.000

lb/mmBtuO2 7.52E-13 1.36E-12 1.67E-12 0.000

ng/dscm 8.53E-04 1.52E-03 1.88E-03 0.001

ng/dscm@7%O2 8.72E-04 1.58E-03 1.94E-03 0.001

Compound: Other TCDF

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.00000000986 0.0000000656 0.0000000508 0.000

lb/mmBtuO2 9.17E-13 5.98E-12 4.85E-12 0.000

ng/dscm 1.04E-03 6.69E-03 5.46E-03 0.004

ng/dscm@7%O2 1.06E-03 6.94E-03 5.62E-03 0.005

Location: Duct near stack breaching - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run NPT3 R1N NPT3 R1S NPT3 R2N

Elb/hr 4.73E-01 8.08E-01 4.81E-01 0.587

gr/dscf 1.60E-04 2.40E-04 1.60E-04 0.000

lb/mmBtuO2 3.33E-04 4.96E-04 3.55E-04 0.000

mg/dscm 3.67E-01 5.50E-01 3.67E-01 0.428

ppm 2.00E-01 3.00E-01 2.00E-01 0.233

ppm@7%O2 2.11E-01 3.14E-01 2.24E-01 0.250

Monday, February 28, 2011 Page 25 of 52
Northport Unit 3 ICR Test Program

Location: Duct near stack breaching - Method 25A 3

Compound: Total organic compounds (TOC) as 

Average

Run NPT3 R2S NPT3 R3N NPT3 R3S

Elb/hr 7.94E-01 1.71E+00 4.03E+00 2.178

gr/dscf 2.40E-04 5.61E-04 1.28E-03 0.001

lb/mmBtuO2 5.23E-04 1.25E-03 2.86E-03 0.002

mg/dscm 5.50E-01 1.28E+00 2.93E+00 1.587

ppm 3.00E-01 7.00E-01 1.60E+00 0.867

ppm@7%O2 3.31E-01 7.91E-01 1.81E+00 0.977

Location: Duct near stack breaching - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.8 0.69 1 0.830

Elb/hr 2.55E-01 2.55E-01 3.31E-01 0.280

lb/mmBtuO2 1.86E-04 2.02E-04 2.22E-04 0.000

mg/dscm 2.03E-01 2.30E-01 2.48E-01 0.227

mg/dscm@7%O2 2.15E-01 2.33E-01 2.57E-01 0.235

Compound: Hydrogen Fluoride

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.63 0.44 0.52 0.530

Elb/hr 2.01E-01 1.62E-01 1.72E-01 0.178

lb/mmBtuO2 1.47E-04 1.29E-04 1.16E-04 0.000

mg/dscm 1.60E-01 1.47E-01 1.29E-01 0.145

mg/dscm@7%O2 1.70E-01 1.49E-01 1.34E-01 0.151

Location: Duct near stack breaching - Method 26A 3

Compound: Hydrogen Chloride

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.84 1.14 0.79 0.923

Elb/hr 3.16E-01 3.73E-01 2.98E-01 0.329

lb/mmBtuO2 2.25E-04 2.62E-04 1.99E-04 0.000

mg/dscm 2.53E-01 2.98E-01 2.22E-01 0.258

mg/dscm@7%O2 2.60E-01 3.05E-01 2.30E-01 0.265

Compound: Hydrogen Fluoride

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.47 0.61 0.53 0.537

Elb/hr 1.77E-01 1.99E-01 2.00E-01 0.192

lb/mmBtuO2 1.26E-04 1.40E-04 1.33E-04 0.000

mg/dscm 1.41E-01 1.59E-01 1.49E-01 0.150

mg/dscm@7%O2 1.45E-01 1.63E-01 1.55E-01 0.154

Location: Duct near stack breaching - Method 29 

Monday, February 28, 2011 Page 26 of 52
Northport Unit 3 ICR Test Program

Compound: Antimony

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.12776 0.14392 0.1488 0.140

Elb/hr 2.43E-02 2.67E-02 2.88E-02 0.027

lb/mmBtuO2 1.98E-05 2.18E-05 2.47E-05 0.000

mg/dscm 1.98E-02 2.15E-02 2.33E-02 0.022

mg/dscm@7%O2 2.29E-02 2.53E-02 2.87E-02 0.026

Compound: Arsenic

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.00443 0.00424 0.00441 0.004

Elb/hr 8.42E-04 7.85E-04 8.53E-04 0.001

lb/mmBtuO2 6.85E-07 6.43E-07 7.31E-07 0.000

mg/dscm 6.86E-04 6.33E-04 6.89E-04 0.001

mg/dscm@7%O2 7.95E-04 7.46E-04 8.48E-04 0.001

Compound: Beryllium

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.000275 0.000289 0.000315 0.000

Elb/hr 5.23E-05 5.35E-05 6.09E-05 0.000

lb/mmBtuO2 4.25E-08 4.38E-08 5.22E-08 0.000

mg/dscm 4.26E-05 4.32E-05 4.92E-05 0.000

mg/dscm@7%O2 4.93E-05 5.09E-05 6.05E-05 0.000

Compound: Cadmium

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.000622 0.000484 0.000408 0.001

Elb/hr 1.18E-04 8.96E-05 7.89E-05 0.000

lb/mmBtuO2 9.62E-08 7.34E-08 6.77E-08 0.000

mg/dscm 9.63E-05 7.23E-05 6.38E-05 0.000

mg/dscm@7%O2 1.12E-04 8.52E-05 7.85E-05 0.000

Compound: Chromium

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.00757 0.01454 0.01379 0.012

Elb/hr 1.44E-03 2.69E-03 2.67E-03 0.002

lb/mmBtuO2 1.17E-06 2.21E-06 2.29E-06 0.000

mg/dscm 1.17E-03 2.17E-03 2.16E-03 0.002

mg/dscm@7%O2 1.36E-03 2.56E-03 2.66E-03 0.002

Compound: Filterable Particulate

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 50.7 138.9 46.7 78.767

Elb/hr 9.64E+00 2.57E+01 9.03E+00 14.790

lb/mmBtuO2 7.84E-03 2.11E-02 7.74E-03 0.012

mg/dscm 7.85E+00 2.07E+01 7.30E+00 11.950

mg/dscm@7%O2 9.09E+00 2.44E+01 8.98E+00 14.157

Monday, February 28, 2011 Page 27 of 52
Northport Unit 3 ICR Test Program

Compound: Lead

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.01119 0.010952 0.00934 0.010

Elb/hr 2.13E-03 2.03E-03 1.81E-03 0.002

lb/mmBtuO2 1.73E-06 1.66E-06 1.55E-06 0.000

mg/dscm 1.73E-03 1.64E-03 1.46E-03 0.002

mg/dscm@7%O2 2.00E-03 1.93E-03 1.80E-03 0.002

Compound: Manganese

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.56245 0.73546 0.6902 0.663

Elb/hr 1.07E-01 1.36E-01 1.33E-01 0.125

lb/mmBtuO2 8.70E-05 1.12E-04 1.14E-04 0.000

mg/dscm 8.71E-02 1.10E-01 1.08E-01 0.102

mg/dscm@7%O2 1.01E-01 1.30E-01 1.33E-01 0.121

Compound: Nickel

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.76901 0.8566 0.969 0.865

Elb/hr 1.46E-01 1.59E-01 1.87E-01 0.164

lb/mmBtuO2 1.19E-04 1.30E-04 1.61E-04 0.000

mg/dscm 1.19E-01 1.28E-01 1.51E-01 0.133

mg/dscm@7%O2 1.38E-01 1.51E-01 1.86E-01 0.158

Compound: Selenium

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 0.00658 0.00755 0.006577 0.007

Elb/hr 1.25E-03 1.40E-03 1.27E-03 0.001

lb/mmBtuO2 1.02E-06 1.15E-06 1.09E-06 0.000

mg/dscm 1.02E-03 1.13E-03 1.03E-03 0.001

mg/dscm@7%O2 1.18E-03 1.33E-03 1.27E-03 0.001

Location: Duct near stack breaching - Method 29 3

Compound: Antimony

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.2988 0.12767 0.491784 0.306

Elb/hr 5.39E-02 2.40E-02 8.83E-02 0.055

lb/mmBtuO2 3.43E-05 1.83E-05 5.48E-05 0.000

mg/dscm 3.92E-02 1.97E-02 6.22E-02 0.040

mg/dscm@7%O2 3.98E-02 2.12E-02 6.36E-02 0.042

Compound: Arsenic

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.0083 0.00463 0.01206 0.008

Elb/hr 1.50E-03 8.72E-04 2.16E-03 0.002

lb/mmBtuO2 9.54E-07 6.63E-07 1.34E-06 0.000

mg/dscm 1.09E-03 7.13E-04 1.52E-03 0.001

Monday, February 28, 2011 Page 28 of 52
Northport Unit 3 ICR Test Program

mg/dscm@7%O2 1.11E-03 7.68E-04 1.55E-03 0.001

Compound: Beryllium

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.000769 0.000311 0.00128 0.001

Elb/hr 1.39E-04 5.85E-05 2.30E-04 0.000

lb/mmBtuO2 8.84E-08 4.45E-08 1.43E-07 0.000

mg/dscm 1.01E-04 4.79E-05 1.62E-04 0.000

mg/dscm@7%O2 1.02E-04 5.16E-05 1.66E-04 0.000

Compound: Cadmium

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.000657 0.000608 0.001095 0.001

Elb/hr 1.18E-04 1.14E-04 1.97E-04 0.000

lb/mmBtuO2 7.55E-08 8.71E-08 1.22E-07 0.000

mg/dscm 8.63E-05 9.37E-05 1.38E-04 0.000

mg/dscm@7%O2 8.76E-05 1.01E-04 1.41E-04 0.000

Compound: Chromium

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.0238 0.01028 0.015152 0.016

Elb/hr 4.29E-03 1.94E-03 2.72E-03 0.003

lb/mmBtuO2 2.74E-06 1.47E-06 1.69E-06 0.000

mg/dscm 3.13E-03 1.58E-03 1.92E-03 0.002

mg/dscm@7%O2 3.18E-03 1.70E-03 1.96E-03 0.002

Compound: Filterable Particulate

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 212.3 85.5 333.8 210.533

Elb/hr 3.83E+01 1.61E+01 5.99E+01 38.100

lb/mmBtuO2 2.44E-02 1.22E-02 3.72E-02 0.025

mg/dscm 2.79E+01 1.32E+01 4.22E+01 27.767

mg/dscm@7%O2 2.83E+01 1.42E+01 4.31E+01 28.533

Compound: Lead

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.0214 0.007814 0.029297 0.020

Elb/hr 3.86E-03 1.47E-03 5.26E-03 0.004

lb/mmBtuO2 2.46E-06 1.12E-06 3.26E-06 0.000

mg/dscm 2.81E-03 1.20E-03 3.70E-03 0.003

mg/dscm@7%O2 2.85E-03 1.29E-03 3.78E-03 0.003

Compound: Manganese

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 1.5744 0.6726 2.93001 1.726

Elb/hr 2.84E-01 1.27E-01 5.26E-01 0.312

lb/mmBtuO2 1.81E-04 9.63E-05 3.27E-04 0.000

mg/dscm 2.07E-01 1.04E-01 3.70E-01 0.227

Monday, February 28, 2011 Page 29 of 52
Northport Unit 3 ICR Test Program

mg/dscm@7%O2 2.10E-01 1.12E-01 3.78E-01 0.233

Compound: Nickel

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 2.022 0.8518 3.64078 2.172

Elb/hr 3.65E-01 1.60E-01 6.54E-01 0.393

lb/mmBtuO2 2.32E-04 1.22E-04 4.06E-04 0.000

mg/dscm 2.66E-01 1.31E-01 4.60E-01 0.286

mg/dscm@7%O2 2.70E-01 1.41E-01 4.70E-01 0.294

Compound: Selenium

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 0.01003 0.00419 0.00915 0.008

Elb/hr 1.81E-03 7.89E-04 1.64E-03 0.001

lb/mmBtuO2 1.15E-06 6.00E-07 1.02E-06 0.000

mg/dscm 1.32E-03 6.46E-04 1.16E-03 0.001

mg/dscm@7%O2 1.34E-03 6.96E-04 1.19E-03 0.001

Location: Duct near stack breaching - Method 6C

Compound: Sulfur Dioxide

Average

Run NPT3 R1N NPT3 R1S NPT3 R2N

Elb/hr 7.82E+02 7.81E+02 9.36E+02 833.000

lb/mmBtuO2 5.71E-01 6.19E-01 6.29E-01 0.606

mg/dscm 6.24E+02 7.07E+02 7.03E+02 678.000

mg/dscm@7%O2 6.62E+02 7.17E+02 7.29E+02 702.667

ppm 2.34E+02 2.65E+02 2.64E+02 254.333

ppm@7%O2 2.48E+02 2.69E+02 2.74E+02 263.667

Location: Duct near stack breaching - Method 6C 3

Compound: Sulfur Dioxide

Average

Run NPT3 R2S NPT3 R3N NPT3 R3S

Elb/hr 9.15E+02 9.09E+02 9.69E+03 3,838.000

lb/mmBtuO2 6.49E-01 6.40E-01 6.45E-01 0.645

mg/dscm 7.31E+02 7.26E+02 7.21E+02 726.000

mg/dscm@7%O2 7.53E+02 7.42E+02 7.48E+02 747.667

ppm 2.75E+02 2.73E+02 2.71E+02 273.000

ppm@7%O2 2.83E+02 2.79E+02 2.81E+02 281.000

Location: Duct near stack breaching - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run NPT3 R1N NPT3 R1S NPT3 R2N

Elb/hr 2.87E+02 2.16E+02 3.41E+02 281.333

lb/mmBtuO2 2.09E-01 1.71E-01 2.29E-01 0.203

mg/dscm 2.29E+02 1.95E+02 2.56E+02 226.667

mg/dscm@7%O2 2.43E+02 1.98E+02 2.66E+02 235.667

ppm 1.20E+02 1.02E+02 1.34E+02 118.667

ppm@7%O2 1.27E+02 1.03E+02 1.39E+02 123.000

Monday, February 28, 2011 Page 30 of 52
Northport Unit 3 ICR Test Program

Location: Duct near stack breaching - Method 7E 3

Compound: Nitrogen oxides (NOx)

Average

Run NPT3 R2S NPT3 R3N NPT3 R3S

Elb/hr 2.75E+02 2.32E+02 2.68E+02 258.333

lb/mmBtuO2 1.95E-01 1.64E-01 1.78E-01 0.179

mg/dscm 2.19E+02 1.86E+02 1.99E+02 201.333

mg/dscm@7%O2 2.25E+02 1.90E+02 2.06E+02 207.000

ppm 1.15E+02 9.71E+01 1.04E+02 105.367

ppm@7%O2 1.18E+02 9.92E+01 1.08E+02 108.400

Location: Duct near stack breaching - OTM - 27/28

Compound: Filterable PM2.5

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 11.9 8.6 9.4 9.967

lb/mmBtuO2 2.78E-03 1.85E-03 2.28E-03 0.002

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 87.5 54.7 4.1 48.767

lb/mmBtuO2 2.05E-02 1.18E-02 9.93E-04 0.011

Compound: Organic Condensible Particulate

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 5.1 5.1 93.1 34.433

lb/mmBtuO2 1.19E-03 1.10E-03 2.26E-02 0.008

Compound: Total PM2.5

Average

RunNumber NPT3 R1N NPT3 R1S NPT3 R2N

Mass_mg 104.5 68.4 106.6 93.167

lb/mmBtuO2 2.44E-02 1.47E-02 2.58E-02 0.022

Location: Duct near stack breaching - OTM - 27/28 3

Compound: Filterable PM2.5

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 11.3 10.8 28.1 16.733

lb/mmBtuO2 2.05E-03 2.28E-03 5.32E-03 0.003

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 43.6 53.5 63.5 53.533

lb/mmBtuO2 7.92E-03 1.13E-02 1.20E-02 0.010

Compound: Organic Condensible Particulate

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Monday, February 28, 2011 Page 31 of 52
Northport Unit 3 ICR Test Program

Process Run Data

Mass_mg 5.5 1.9 9.2 5.533

lb/mmBtuO2 9.99E-04 4.00E-04 1.74E-03 0.001

Compound: Total PM2.5

Average

RunNumber NPT3 R2S NPT3 R3N NPT3 R3S

Mass_mg 60.4 66.2 100.8 75.800

lb/mmBtuO2 1.10E-02 1.40E-02 1.91E-02 0.015

Monday, February 28, 2011 Page 32 of 52
Northport Unit 3 ICR Test Program

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input 0 Million Btus 0

2 Heat Input 0 Million Btus 0

3 Heat Input 0 Million Btus 0

1 Average Heat Input 0 MMBtu/hr 0

2 Average Heat Input 0 MMBtu/hr 0

3 Average Heat Input 0 MMBtu/hr 0

1 Steam Output 0 1000 lb steam/hr 0

2 Steam Output 0 1000 lb steam/hr 0

3 Steam Output 0 1000 lb steam/hr 0

1 Synfuel Firing Rate 0 0

2 Synfuel Firing Rate 0 0

3 Synfuel Firing Rate 0 0

1 Petroleum Coke Firing Rate 0 0

2 Petroleum Coke Firing Rate 0 0

3 Petroleum Coke Firing Rate 0 0

1 Coal Gas Firing Rate 0 0

2 Coal Gas Firing Rate 0 0

3 Coal Gas Firing Rate 0 0

1 Fuel Oil Firing Rate 0 gpm 0

2 Fuel Oil Firing Rate 0 gpm 0

3 Fuel Oil Firing Rate 0 gpm 0

1 Flue Gas Flow Rate 0 dscfm 0

1 Pressure Drop Across FGD (if applicable) 0 in H20 0

1 FGD Scrubber Liquor pH 0 pH 0

1 FGD Scrubber Liquor Flow Rate 0 gal/min 0

1 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

1 Flue Gas Oxygen Content 0 % 0

1 Flue Gas Carbon Dioxide Content 0 % 0

1 Flue Gas Moisture Content 0 % 0

1 Flue Gas Sampling Point Temperature 0 Deg F 0

1 Flue Gas Pressure 0 atm 0

1 Standard Pressure 0 atm 0

1 Standard Temperature 0 Deg F 0

Monday, February 28, 2011 Page 33 of 52
Northport Unit 3 ICR Test Program

APCD Run Data

Process Lab Run Data

1 Unit Gross Electrical Output 0 MW 0

1 Unit Net Electric Generation 0 MWh 0

Run Name Value UOM Comments

Target

Value

1 ELECTROSTATIC PRECIPITATOR 0 0

1 0 0

1 0 0

Run Name Value UOM Comments

1 See 4b Comments. 0

Monday, February 28, 2011 Page 34 of 52
Northport Unit 3 ICR Test Program

Sampling / Stack Data Results Detail

Location Duct near stack breaching - Method 0011

Average

Run Number NPT3 R1N NPT3 R1S NPT3 R2N

Test Date 6/12/2010 6/19/2010 6/19/2010

Run Start Time 6/19/2010 

8:05:00 AM

6/19/2010 

8:05:00 AM

6/19/2010 

11:30:00 AM

Run Finish Time 6/19/2010 

10:29:00 AM

6/19/2010 

10:29:00 AM

6/19/2010 

1:56:00 PM

Net Traversing Points 24 24 24

Net Run Time, minutes 120 120 120

Nozzle Diameter, inches 0.197 0.197 0.197 0.197

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.03 0.99 1.03 1.017

Barometric Pressure, inches of Mercury 30.02 30.02 30.02 30.020

Average Orifice Meter Differential, inches H2O 1.80 2.51 1.89 2.067

Dry Gas Meter Volume Sampled, cubic feet 89.410 101.911 89.764 93.695

Average Dry Gas Meter Temperature, °F 83.38 76.50 94.42 84.767

Dry Gas Meter Volume Sampled, dscf 90.181 100.238 88.754 93.058

Total Moisture Liquid collected, g 160.1 191.2 160.3 170.533

Volume of Water Vapor, standard cubic feet 7.54 9.00 7.55 8.030

Moisture Content of Stack Gas, % 7.72 8.24 7.84 7.933

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Dry Mole Fraction 0.9228 0.9176 0.9216 0.921

Carbon Dioxide, % 10.7 10.8 10 10.500

Oxygen, % 7.7 7.6 8.5 7.933

Carbon Monoxide & Nitrogen, % 81.6 81.6 81.5 81.567

Fuel Factor 1.23 1.23 1.24

Dry Molecular Weight, lb/lb-Mole 30.02 30.03 29.94 29.997

Wet Molecular weight, lb/lb-Mole 29.09 29.04 29.00 29.043

Flue Gas Static Pressure, inches of H2O 1.5 1.1 1.5 1.367

Absolute Flue Gas Pressure, inches of Mercury 30.13 30.10 30.13 30.120

Average Stack Gas Temperature, °F 289.42 303.46 292.58 295.153

Average Velocity Head, inches of H2O 2.0135453473

0279

2.695247460

96668

2.093062065

3772

2.267

Average Stack Gas Velocity, feet/second 94.23 110.18 96.42 100.277

Stack Cross-Sectional Area, square feet 93.000 93.000 93.000 93.000

Dry Volumetric Flow Rate, dry scfm 344,252.5 392,502.9 350,318.1 362,357.833

Actual Wet Volumetric Flue Gas Flow Rate, acfm 525,803.4 614,804.4 538,023.6 559,543.800

Percent Isokinetic of Sampling Rate, % 95.9 93.5 92.8 94.067

Percent Excess Air, % 55.6 54.5 65.3 58.467

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

Round Duct Diameter, inches 0 0 0

Rectangular Duct Width, inches 124 124 124

Rectangular Duct Length, inches 108 108 108

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 28, 2011 Page 35 of 52
Northport Unit 3 ICR Test Program

Location Duct near stack breaching - Method 0011 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Monday, February 28, 2011 Page 36 of 52
Northport Unit 3 ICR Test Program

Location Duct near stack breaching - Method 10

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Monday, February 28, 2011 Page 37 of 52
Northport Unit 3 ICR Test Program

Location Duct near stack breaching - Method 10 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Monday, February 28, 2011 Page 38 of 52
Northport Unit 3 ICR Test Program

Location Duct near stack breaching - Method 23

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Monday, February 28, 2011 Page 39 of 52
Northport Unit 3 ICR Test Program

Location Duct near stack breaching - Method 23 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Monday, February 28, 2011 Page 40 of 52
Northport Unit 3 ICR Test Program

Location Duct near stack breaching - Method 25A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Monday, February 28, 2011 Page 41 of 52
Northport Unit 3 ICR Test Program

Location Duct near stack breaching - Method 25A 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Monday, February 28, 2011 Page 42 of 52
Northport Unit 3 ICR Test Program

Location Duct near stack breaching - Method 26A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Monday, February 28, 2011 Page 43 of 52
Northport Unit 3 ICR Test Program

Location Duct near stack breaching - Method 26A 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Monday, February 28, 2011 Page 44 of 52
Northport Unit 3 ICR Test Program

Location Duct near stack breaching - Method 29 

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Monday, February 28, 2011 Page 45 of 52
Northport Unit 3 ICR Test Program

Location Duct near stack breaching - Method 29 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Monday, February 28, 2011 Page 46 of 52
Northport Unit 3 ICR Test Program

Location Duct near stack breaching - Method 6C

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Monday, February 28, 2011 Page 47 of 52
Northport Unit 3 ICR Test Program

Location Duct near stack breaching - Method 6C 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Monday, February 28, 2011 Page 48 of 52
Northport Unit 3 ICR Test Program

Location Duct near stack breaching - Method 7E

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Monday, February 28, 2011 Page 49 of 52
Northport Unit 3 ICR Test Program

Location Duct near stack breaching - Method 7E 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Monday, February 28, 2011 Page 50 of 52
Northport Unit 3 ICR Test Program

Location Duct near stack breaching - OTM - 27/28

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Monday, February 28, 2011 Page 51 of 52
Northport Unit 3 ICR Test Program

Location Duct near stack breaching - OTM - 27/28 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Monday, February 28, 2011 Page 52 of 52