Name:

Title:

Company:

Sign Date:

Name:

Title:

Company:

Sign Date:

Permitted Facility Representative / Date Testing Company Representative / Date

Port Jefferson Unit 4 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 28
Port Jefferson Unit 4 ICR Test Program

Facility Information:

Port Jefferson

North End Beach Street

Port Jefferson NY 11777

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:

1-4722-00107/00035

Permitted Source ID/Name:

U-00003 Boiler 4

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 185 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

Stack Platform 252 252 0 0 2600 2000 4 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Platform % H2O Method 1 - 4 3 180 0

Stack Platform Carbon Monoxide Method 10 3 120 0

Stack Platform Formaldehyde Method 0011 3 120 0

Stack Platform 2,3,7,8-TCDD Method 23 3 480 0

Stack Platform 1,2,3,7,8-PeCDD Method 23 3 480 0

Regulation Description Compound Limit Unit

0

Monday, February 28, 2011 Page 2 of 28
Port Jefferson Unit 4 ICR Test Program

Stack Platform OCDD Method 23 3 480 0

Stack Platform 2,3,7,8-TCDF Method 23 3 480 0

Stack Platform 1,2,3,7,8-PeCDF Method 23 3 480 0

Stack Platform 2,3,4,7,8-PeCDF Method 23 3 480 0

Stack Platform 1,2,3,4,6,7,8-HpCDF Method 23 3 480 0

Stack Platform OCDF Method 23 3 480 0

Stack Platform Other TCDD Method 23 3 480 0

Stack Platform Other PeCDD Method 23 3 480 0

Stack Platform Other HxCDD Method 23 3 480 0

Stack Platform Other HpCDD Method 23 3 480 0

Stack Platform Other TCDF Method 23 3 480 0

Stack Platform Other PeCDF Method 23 3 480 0

Stack Platform Other HxCDF Method 23 3 480 0

Stack Platform Other HpCDF Method 23 3 480 0

Stack Platform 3,3',4,4'-TCB (PCB77) Method 23 3 480 0

Stack Platform 3,4,4',5-TCB (PCB81) Method 23 3 480 0

Stack Platform 2,3,3',4,4'-PeCB (PCB105) Method 23 3 480 0

Stack Platform 2,3,4,4',5-PeCB (PCB114) Method 23 3 480 0

Stack Platform 2,3',4,4',5-PeCB (PCB118) Method 23 3 480 0

Stack Platform 2',3,4,4',5-PeCB (PCB123) Method 23 3 480 0

Stack Platform 3,3',4,4',5-PeCB (PCB126) Method 23 3 480 0

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

HxCB (PCBs156/157)

Stack Platform Method 23 3 480 0

Stack Platform 2,3',4,4',5,5'-HxCB (PCB167) Method 23 3 480 0

Stack Platform 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 480 0

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

(PCB189)

Stack Platform Method 23 3 480 0

Total organic compounds 

(TOC) as Propane

Stack Platform Method 25A 3 120 0

Stack Platform Hydrogen Fluoride Method 26A 3 180 0

Stack Platform Hydrogen Chloride Method 26A 3 180 0

Stack Platform Hydrogen Chloride Method 26 3 180 0

Stack Platform Hydrogen Fluoride Method 26 3 180 0

Stack Platform Filterable PM2.5 OTM - 27/28 3 364 0

Inorganic (Aqueous) 

Condensible Part.

Stack Platform OTM - 27/28 3 364 0

Organic Condensible 

Particulate

Stack Platform OTM - 27/28 3 364 0

Stack Platform Total PM2.5 OTM - 27/28 3 364 0

Stack Platform Filterable Particulate Method 29 3 240 0

Stack Platform Antimony Method 29 3 240 0

Stack Platform Manganese Method 29 3 240 0

Stack Platform Cadmium Method 29 3 240 0

Stack Platform Selenium Method 29 3 240 0

Stack Platform Lead Method 29 3 240 0

Stack Platform Chromium Method 29 3 240 0

Stack Platform Arsenic Method 29 3 240 0

Stack Platform Beryllium Method 29 3 240 0

Stack Platform Nickel Method 29 3 240 0

Stack Platform O2 Method 3A O2 3 480 0

Stack Platform Co2 Method 3A CO2 3 480 0

Stack Platform O2 Method 3A O2 3 120 0

Stack Platform Co2 Method 3A CO2 3 120 0

Monday, February 28, 2011 Page 3 of 28
Port Jefferson Unit 4 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.

No modification and/or deviations from applicable test methods.

Stack Platform O2 Method 3A O2 3 240 0

Stack Platform Co2 Method 3A CO2 3 240 0

Stack Platform Filterable Particulate Method 5 3 240 0

Stack Platform Sulfur Dioxide Method 6C 3 180 0

Stack Platform Nitrogen oxides (NOx) Method 7E 3 180 0

Monday, February 28, 2011 Page 4 of 28
Port Jefferson Unit 4 ICR Test Program

Sampling / Stack Data Results Summary

Location Stack Platform - Method 0011

Average

Run Number PJ4 R1 PJ4 R2 PJ4 R3

Test Date 7/15/2010 7/15/2010 7/15/2010

Run Start Time 7/15/2010 

8:20:00 AM

7/15/2010 

11:10:00 

AM

7/15/2010 

1:50:00 PM

Run Finish Time 7/15/2010 

10:36:00 AM

7/15/2010 

1:24:00 PM

7/15/2010 

4:02:00 PM

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 80.779 80.141 82.980 81.300

Moisture Content of Stack Gas, % 8.51 8.56 8.34 8.470

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

Carbon Dioxide, % 10.07 10.05 10.02 10.047

Oxygen, % 8.4 8.34 8.31 8.350

Average Stack Gas Temperature, °F 305.00 305.00 305.00 305.000

Dry Volumetric Flow Rate, dry scfm 1,467,368.1 1,467,393.4 1,470,387.1 1,468,382.86

7

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,278,085.6 2,277,877.8 2,277,046.5 2,277,669.96

7

Percent Isokinetic of Sampling Rate, % 100.8 100.0 103.3 101.367

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

Location Stack Platform - Method 10

Average

Run Number PJ4 R1 PJ4 R2 PJ4 R3

Test Date 7/12/2010 7/13/2010 7/14/2010

Run Start Time 8:10:00 AM 8:00:00 

AM

7:50:00 AM

Run Finish Time 4:30:00 PM 4:04:00 PM 4:14:00 PM

Carbon Dioxide, % 10.38 10.26 10.2 10.280

Oxygen, % 7.8 7.94 8.13 7.957

Dry Volumetric Flow Rate, dry scfm 1461270.4 1451609.6 1467890.8 1,460,256.93

3

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

Moisture, % 8.73 9.14 9.14 9.003

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 28, 2011 Page 5 of 28
Port Jefferson Unit 4 ICR Test Program

Location Stack Platform - Method 23

Average

Run Number PJ4 R1 PJ4 R2 PJ4 R3

Test Date 7/12/2010 7/13/2010 7/14/2010

Run Start Time 7/12/2010 

8:10:00 AM

7/13/2010 

8:00:00 

AM

7/14/2010 

7:50:00 AM

Run Finish Time 7/12/2010 

4:30:00 PM

7/13/2010 

4:04:00 PM

7/14/2010 

4:14:00 PM

Net Run Time, minutes 480 480 480

Dry Gas Meter Volume Sampled, dscf 310.593 311.569 310.184 310.782

Moisture Content of Stack Gas, % 8.73 9.14 9.20 9.023

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

Carbon Dioxide, % 10.38 10.26 10.2 10.280

Oxygen, % 7.8 7.94 8.13 7.957

Average Stack Gas Temperature, °F 307.17 307.17 307.17 307.170

Dry Volumetric Flow Rate, dry scfm 1,461,767.4 1,457,643.1 1,455,742.7 1,458,384.40

0

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,288,060.8 2,288,892.0 2,291,178.0 2,289,376.93

3

Percent Isokinetic of Sampling Rate, % 97.3 97.9 97.5 97.567

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

Location Stack Platform - Method 25A

Average

Run Number PJ4 R1 PJ4 R2 PJ4 R3

Test Date 7/15/2010 7/15/2010 7/15/2010

Run Start Time 8:20:00 AM 11:10:00 

AM

1:50:00 PM

Run Finish Time 10:36:00 AM 1:24:00 PM 4:02:00 PM

Carbon Dioxide, % 10.04 10.05 10.02 10.037

Oxygen, % 8.4 8.34 8.31 8.350

Dry Volumetric Flow Rate, dry scfm 1466967.4 1472996.6 1478011.5 1,472,658.50

0

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

Moisture, % 8.5 8.64 8.5 8.547

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 28, 2011 Page 6 of 28
Port Jefferson Unit 4 ICR Test Program

Location Stack Platform - Method 26A

Average

Run Number PJ4 R1 PJ4 R2 PJ4 R3

Test Date 7/12/2010 7/12/2010 7/12/2010

Run Start Time 7/12/2010 

8:10:00 AM

7/12/2010 

12:13:00 

PM

7/12/2010 

4:00:00 PM

Run Finish Time 7/12/2010 

11:31:00 AM

7/12/2010 

3:34:00 PM

7/12/2010 

7:15:00 PM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 126.471 124.813 123.525 124.936

Moisture Content of Stack Gas, % 9.01 8.28 8.54 8.610

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

Carbon Dioxide, % 10.27 10.51 10.35 10.377

Oxygen, % 7.9 7.75 7.74 7.797

Average Stack Gas Temperature, °F 304.25 309.50 308.33 307.360

Dry Volumetric Flow Rate, dry scfm 1,527,025.0 1,510,576.0 1,493,724.5 1,510,441.83

3

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,388,436.2 2,342,300.9 2,337,521.1 2,356,086.06

7

Percent Isokinetic of Sampling Rate, % 101.1 100.9 101.0 101.000

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 28
Port Jefferson Unit 4 ICR Test Program

Location Stack Platform - Method 29 

Average

Run Number PJ4 R1 PJ4 R2 PJ4 R3

Test Date 7/13/2010 7/14/2010 7/14/2010

Run Start Time 7/13/2010 

8:00:00 AM

7/14/2010 

7:50:00 

AM

7/14/2010 

3:50:00 PM

Run Finish Time 7/13/2010 

2:12:00 PM

7/14/2010 

2:22:00 PM

7/14/2010 

10:15:00 PM

Net Run Time, minutes 360 360 360

Dry Gas Meter Volume Sampled, dscf 241.709 241.959 247.005 243.558

Moisture Content of Stack Gas, % 9.18 9.64 9.36 9.393

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

Carbon Dioxide, % 10.25 10.23 10.17 10.217

Oxygen, % 7.96 8.11 8.15 8.073

Average Stack Gas Temperature, °F 310.50 310.50 312.17 311.057

Dry Volumetric Flow Rate, dry scfm 1,455,182.8 1,447,922.3 1,471,408.3 1,458,171.13

3

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,295,957.8 2,299,906.3 2,332,741.3 2,309,535.13

3

Percent Isokinetic of Sampling Rate, % 101.4 102.0 102.5 101.967

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

Location Stack Platform - Method 6C

Average

Run Number PJ4 R1 PJ4 R2 PJ4 R3

Test Date 7/12/2010 7/12/2010 7/12/2010

Run Start Time 8:10:00 AM 12:13:00 

PM

4:00:00 PM

Run Finish Time 11:31:00 AM 3:34:00 PM 7:15:00 PM

Carbon Dioxide, % 10.27 10.51 10.35 10.377

Oxygen, % 7.9 7.75 7.74 7.797

Dry Volumetric Flow Rate, dry scfm 1526487.8 1503903.7 1493267.3 1,507,886.26

7

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

Moisture, % 9.01 8.34 8.55 8.633

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 28, 2011 Page 8 of 28
Port Jefferson Unit 4 ICR Test Program

Location Stack Platform - Method 7E

Average

Run Number PJ4 R1 PJ4 R2 PJ4 R3

Test Date 7/12/2010 7/12/2010 7/12/2010

Run Start Time 8:10:00 AM 12:13:00 

PM

4:00:00 PM

Run Finish Time 11:31:00 AM 3:34:00 PM 7:15:00 PM

Carbon Dioxide, % 10.27 10.51 10.35 10.377

Oxygen, % 7.9 7.75 7.74 7.797

Dry Volumetric Flow Rate, dry scfm 1526487.8 1503903.7 1493267 1,507,886.16

7

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

Moisture, % 9.01 8.34 8.55 8.633

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Location Stack Platform - OTM - 27/28

Average

Run Number PJ4 R1 PJ4 R2 PJ4 R3

Test Date 7/13/2010 7/14/2010 7/14/2010

Run Start Time 7/13/2010 

8:00:00 AM

7/14/2010 

7:50:00 

AM

7/14/2010 

3:50:00 PM

Run Finish Time 7/13/2010 

2:15:00 PM

7/14/2010 

2:22:00 PM

7/14/2010 

10:15:00 PM

Net Run Time, minutes 359.08 365.41 360.66

Dry Gas Meter Volume Sampled, dscf 143.878 146.151 144.925 144.985

Moisture Content of Stack Gas, % 8.51 8.88 9.11 8.833

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

Carbon Dioxide, % 30.25 10.17 10.23 16.883

Oxygen, % 7.96 8.15 8.11 8.073

Average Stack Gas Temperature, °F 307.75 307.75 309.83 308.443

Dry Volumetric Flow Rate, dry scfm 1,392,736.6 1,455,664.9 1,460,174.9 1,436,192.13

3

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,173,553.8 2,284,735.7 2,301,568.8 2,253,286.10

0

Percent Isokinetic of Sampling Rate, % 108.1 103.2 103.4 104.900

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 9 of 28
Port Jefferson Unit 4 ICR Test Program

Emissions Summary

Location: Stack Platform - Method 0011

Compound: Formaldehyde

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.0153 0.0109 0.0076 0.011

lb/mmBtuO2 6.42E-06 4.59E-06 3.08E-06 0.000

ppm 5.36E-03 3.85E-03 2.59E-03 0.004

ppm@7%O2 5.96E-03 4.26E-03 2.86E-03 0.004

Location: Stack Platform - Method 10

Compound: Carbon Monoxide

Average

Run PJ4 R1 PJ4 R2 PJ4 R3

Elb/hr 2.56E+00 4.43E+00 3.86E+00 3.617

lb/mmBtuO2 4.29E-04 7.55E-04 6.60E-04 0.001

mg/dscm 4.69E-01 8.16E-01 7.03E-01 0.663

Location: Stack Platform - Method 23

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

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.00000000501 0.00000000531 0.00000000503 0.000

lb/mmBtuO2 5.21E-13 5.57E-13 5.38E-13 0.000

ng/dscm 5.70E-04 6.02E-04 5.73E-04 0.001

ng/dscm@7%O2 6.05E-04 6.46E-04 6.24E-04 0.001

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

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.00000000189 0.00000000179 0.00000000176 0.000

lb/mmBtuO2 1.97E-13 1.88E-13 1.88E-13 0.000

ng/dscm 2.15E-04 2.03E-04 2.00E-04 0.000

ng/dscm@7%O2 2.28E-04 2.18E-04 2.18E-04 0.000

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

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.00000000167 0.00000000177 0.00000000146 0.000

lb/mmBtuO2 1.74E-13 1.86E-13 1.56E-13 0.000

ng/dscm 1.90E-04 2.01E-04 1.66E-04 0.000

ng/dscm@7%O2 2.02E-04 2.16E-04 1.81E-04 0.000

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

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.00000000364 0.00000000619 0.000000006 0.000

lb/mmBtuO2 3.79E-13 6.49E-13 6.41E-13 0.000

ng/dscm 4.14E-04 7.02E-04 6.83E-04 0.001

ng/dscm@7%O2 4.39E-04 7.53E-04 7.43E-04 0.001

Monday, February 28, 2011 Page 10 of 28
Port Jefferson Unit 4 ICR Test Program

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

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.0000001145 0.000000192 0.000000242 0.000

lb/mmBtuO2 1.19E-11 2.01E-11 2.59E-11 0.000

ng/dscm 1.30E-02 2.18E-02 2.76E-02 0.021

ng/dscm@7%O2 1.38E-02 2.34E-02 3.00E-02 0.022

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

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.000000447 0.000000728 0.000000895 0.000

lb/mmBtuO2 4.65E-11 7.63E-11 9.57E-11 0.000

ng/dscm 5.08E-02 8.25E-02 1.02E-01 0.078

ng/dscm@7%O2 5.39E-02 8.85E-02 1.11E-01 0.084

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

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.0000000421 0.0000000787 0.0000000943 0.000

lb/mmBtuO2 4.38E-12 8.25E-12 1.01E-11 0.000

ng/dscm 4.79E-03 8.92E-03 1.07E-02 0.008

ng/dscm@7%O2 5.08E-03 9.57E-03 1.16E-02 0.009

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

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.0000000282 0.0000000526 0.0000000695 0.000

lb/mmBtuO2 2.93E-12 5.52E-12 7.43E-12 0.000

ng/dscm 3.21E-03 5.96E-03 7.91E-03 0.006

ng/dscm@7%O2 3.41E-03 6.39E-03 8.61E-03 0.006

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

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.0000014 0.00000235 0.00000278 0.000

lb/mmBtuO2 1.46E-10 2.46E-10 2.97E-10 0.000

ng/dscm 1.59E-01 2.66E-01 3.17E-01 0.247

ng/dscm@7%O2 1.69E-01 2.85E-01 3.45E-01 0.266

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

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.0000000277 0.0000000543 0.0000000652 0.000

lb/mmBtuO2 2.88E-12 5.69E-12 6.97E-12 0.000

ng/dscm 3.15E-03 6.16E-03 7.42E-03 0.006

ng/dscm@7%O2 3.34E-03 6.61E-03 8.08E-03 0.006

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

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.00000000161 0.00000000171 0.00000000143 0.000

lb/mmBtuO2 1.68E-13 1.79E-13 1.53E-13 0.000

Monday, February 28, 2011 Page 11 of 28
Port Jefferson Unit 4 ICR Test Program

ng/dscm 1.83E-04 1.94E-04 1.63E-04 0.000

ng/dscm@7%O2 1.94E-04 2.08E-04 1.77E-04 0.000

Compound: 2,3,7,8-TCDD

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.00000000125 0.00000000121 0.000000000944 0.000

lb/mmBtuO2 1.30E-13 1.27E-13 1.01E-13 0.000

ng/dscm 1.42E-04 1.37E-04 1.07E-04 0.000

ng/dscm@7%O2 1.51E-04 1.47E-04 1.16E-04 0.000

Compound: 2,3,7,8-TCDF

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.00000000105 0.00000000106 0.000000000977 0.000

lb/mmBtuO2 1.09E-13 1.11E-13 1.04E-13 0.000

ng/dscm 1.19E-04 1.20E-04 1.11E-04 0.000

ng/dscm@7%O2 1.26E-04 1.29E-04 1.21E-04 0.000

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

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.00000000723 0.00000000486 0.00000000626 0.000

lb/mmBtuO2 7.52E-13 5.10E-13 6.69E-13 0.000

ng/dscm 8.22E-04 5.51E-04 7.13E-04 0.001

ng/dscm@7%O2 8.72E-04 5.91E-04 7.76E-04 0.001

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

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.00000000578 0.000000011 0.0000000106 0.000

lb/mmBtuO2 6.02E-13 1.15E-12 1.13E-12 0.000

ng/dscm 6.57E-04 1.25E-03 1.21E-03 0.001

ng/dscm@7%O2 6.97E-04 1.34E-03 1.32E-03 0.001

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

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.0000000981 0.000000163 0.000000161 0.000

lb/mmBtuO2 1.02E-11 1.71E-11 1.72E-11 0.000

ng/dscm 1.12E-02 1.85E-02 1.83E-02 0.016

ng/dscm@7%O2 1.19E-02 1.98E-02 1.99E-02 0.017

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

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.00000000688 0.0000000145 0.0000000119 0.000

lb/mmBtuO2 7.16E-13 1.52E-12 1.27E-12 0.000

ng/dscm 7.82E-04 1.64E-03 1.36E-03 0.001

ng/dscm@7%O2 8.30E-04 1.76E-03 1.48E-03 0.001

Compound: OCDD

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Monday, February 28, 2011 Page 12 of 28
Port Jefferson Unit 4 ICR Test Program

Mass_mg 0.00000847 0.00000000577 0.00000000556 0.000

lb/mmBtuO2 8.81E-10 6.05E-13 5.94E-13 0.000

ng/dscm 9.63E-01 6.54E-04 6.33E-04 0.321

ng/dscm@7%O2 1.02E+00 7.01E-04 6.89E-04 0.340

Compound: OCDF

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.00000522 0.00000000697 0.00000000573 0.000

lb/mmBtuO2 5.43E-10 7.31E-13 6.13E-13 0.000

ng/dscm 5.94E-01 7.90E-04 6.52E-04 0.198

ng/dscm@7%O2 6.30E-01 8.47E-04 7.10E-04 0.211

Compound: Other HpCDD

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

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 HpCDF

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

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 PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0 0.00000000778 0 0.000

lb/mmBtuO2 0.00E+00 8.16E-13 0.00E+00 0.000

ng/dscm 0.00E+00 8.82E-04 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 9.46E-04 0.00E+00 0.000

Compound: Other HxCDF

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0 0.00000000237 0.00000000151 0.000

lb/mmBtuO2 0.00E+00 2.49E-13 1.61E-13 0.000

ng/dscm 0.00E+00 2.69E-04 1.72E-04 0.000

ng/dscm@7%O2 0.00E+00 2.89E-04 1.87E-04 0.000

Compound: Other PeCDD

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0 0.00000000545 0 0.000

lb/mmBtuO2 0.00E+00 5.72E-13 0.00E+00 0.000

ng/dscm 0.00E+00 6.18E-04 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 6.63E-04 0.00E+00 0.000

Monday, February 28, 2011 Page 13 of 28
Port Jefferson Unit 4 ICR Test Program

Compound: Other PeCDF

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

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 TCDD

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0 0.00000000462 0.00000000231 0.000

lb/mmBtuO2 0.00E+00 4.84E-13 2.47E-13 0.000

ng/dscm 0.00E+00 5.24E-04 2.63E-04 0.000

ng/dscm@7%O2 0.00E+00 5.62E-04 2.86E-04 0.000

Compound: Other TCDF

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.00000000284 0.00000000357 0.00000000227 0.000

lb/mmBtuO2 2.96E-13 3.74E-13 2.43E-13 0.000

ng/dscm 3.23E-04 4.05E-04 2.58E-04 0.000

ng/dscm@7%O2 3.43E-04 4.34E-04 2.81E-04 0.000

Location: Stack Platform - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run PJ4 R1 PJ4 R2 PJ4 R3

Elb/hr 3.02E+00 7.08E+00 2.03E+00 4.043

gr/dscf 2.40E-04 5.61E-04 1.60E-04 0.000

lb/mmBtuO2 5.28E-04 1.23E-03 3.49E-04 0.001

mg/dscm 5.50E-01 1.28E+00 3.67E-01 0.732

ppm 3.00E-01 7.00E-01 2.00E-01 0.400

ppm@7%O2 3.34E-01 7.75E-01 2.21E-01 0.443

Location: Stack Platform - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.97 0.99 0.9 0.953

Elb/hr 1.55E+00 1.58E+00 1.44E+00 1.523

lb/mmBtuO2 2.50E-04 2.55E-04 2.34E-04 0.000

mg/dscm 2.71E-01 2.80E-01 2.57E-01 0.269

mg/dscm@7%O2 2.90E-01 2.96E-01 2.71E-01 0.286

Compound: Hydrogen Fluoride

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.4 0.4 0.42 0.407

Elb/hr 6.39E-01 6.40E-01 6.72E-01 0.650

lb/mmBtuO2 1.03E-04 1.03E-04 1.09E-04 0.000

mg/dscm 1.12E-01 1.13E-01 1.20E-01 0.115

Monday, February 28, 2011 Page 14 of 28
Port Jefferson Unit 4 ICR Test Program

mg/dscm@7%O2 1.20E-01 1.19E-01 1.27E-01 0.122

Location: Stack Platform - Method 29 

Compound: Antimony

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 1.184247 1.229485 1.20238 1.205

Elb/hr 9.43E-01 9.73E-01 9.47E-01 0.954

lb/mmBtuO2 1.60E-04 1.68E-04 1.62E-04 0.000

mg/dscm 1.73E-01 1.79E-01 1.72E-01 0.175

mg/dscm@7%O2 1.86E-01 1.95E-01 1.88E-01 0.190

Compound: Arsenic

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.02022 0.01888 0.01881 0.019

Elb/hr 1.61E-02 1.49E-02 1.48E-02 0.015

lb/mmBtuO2 2.74E-06 2.58E-06 2.53E-06 0.000

mg/dscm 2.95E-03 2.76E-03 2.69E-03 0.003

mg/dscm@7%O2 3.17E-03 3.00E-03 2.93E-03 0.003

Compound: Beryllium

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.00172 0.00119 0.00151 0.001

Elb/hr 1.37E-03 9.42E-04 1.19E-03 0.001

lb/mmBtuO2 2.33E-07 1.63E-07 2.03E-07 0.000

mg/dscm 2.51E-04 1.74E-04 2.16E-04 0.000

mg/dscm@7%O2 2.70E-04 1.89E-04 2.35E-04 0.000

Compound: Cadmium

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.001529 0.00125 0.001524 0.001

Elb/hr 1.22E-03 9.89E-04 1.20E-03 0.001

lb/mmBtuO2 2.07E-07 1.71E-07 2.05E-07 0.000

mg/dscm 2.23E-04 1.82E-04 2.18E-04 0.000

mg/dscm@7%O2 2.40E-04 1.98E-04 2.38E-04 0.000

Compound: Chromium

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.06523 0.05429 0.038052 0.053

Elb/hr 5.19E-02 4.30E-02 3.00E-02 0.042

lb/mmBtuO2 8.83E-06 7.43E-06 5.12E-06 0.000

mg/dscm 9.53E-03 7.92E-03 5.44E-03 0.008

mg/dscm@7%O2 1.02E-02 8.61E-03 5.93E-03 0.008

Compound: Filterable Particulate

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 241.5 241.9 226.3 236.567

Elb/hr 1.92E+02 1.91E+02 1.78E+02 187.000

Monday, February 28, 2011 Page 15 of 28
Port Jefferson Unit 4 ICR Test Program

lb/mmBtuO2 3.27E-02 3.31E-02 3.04E-02 0.032

mg/dscm 3.53E+01 3.53E+01 3.24E+01 34.333

mg/dscm@7%O2 3.79E+01 3.84E+01 3.53E+01 37.200

Compound: Lead

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.029889 0.02882 0.029033 0.029

Elb/hr 2.38E-02 2.28E-02 2.29E-02 0.023

lb/mmBtuO2 4.05E-06 3.94E-06 3.90E-06 0.000

mg/dscm 4.37E-03 4.21E-03 4.15E-03 0.004

mg/dscm@7%O2 4.69E-03 4.58E-03 4.52E-03 0.005

Compound: Manganese

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.319968 0.29902 0.293857 0.304

Elb/hr 2.55E-01 2.37E-01 2.32E-01 0.241

lb/mmBtuO2 4.33E-05 4.09E-05 3.95E-05 0.000

mg/dscm 4.68E-02 4.36E-02 4.20E-02 0.044

mg/dscm@7%O2 5.03E-02 4.74E-02 4.58E-02 0.048

Compound: Nickel

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 4.30507 3.96703 4.16365 4.145

Elb/hr 3.43E+00 3.14E+00 3.28E+00 3.283

lb/mmBtuO2 5.83E-04 5.43E-04 5.60E-04 0.001

mg/dscm 6.29E-01 5.79E-01 5.95E-01 0.601

mg/dscm@7%O2 6.76E-01 6.29E-01 6.49E-01 0.651

Compound: Selenium

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 0.03101 0.03352 0.0344 0.033

Elb/hr 2.47E-02 2.65E-02 2.71E-02 0.026

lb/mmBtuO2 4.20E-06 4.59E-06 4.63E-06 0.000

mg/dscm 4.53E-03 4.89E-03 4.92E-03 0.005

mg/dscm@7%O2 4.87E-03 5.31E-03 5.36E-03 0.005

Location: Stack Platform - Method 6C

Compound: Sulfur Dioxide

Average

Run PJ4 R1 PJ4 R2 PJ4 R3

Elb/hr 3.93E+03 4.08E+03 4.09E+03 4,033.333

lb/mmBtuO2 6.34E-01 6.60E-01 6.66E-01 0.653

mg/dscm 6.87E+02 7.24E+02 7.31E+02 714.000

mg/dscm@7%O2 7.35E+02 7.65E+02 7.72E+02 757.333

ppm 2.58E+02 2.72E+02 2.75E+02 268.333

ppm@7%O2 2.76E+02 2.88E+02 2.90E+02 284.667

Location: Stack Platform - Method 7E

Monday, February 28, 2011 Page 16 of 28
Port Jefferson Unit 4 ICR Test Program

Process Run Data

Compound: Nitrogen oxides (NOx)

Average

Run PJ4 R1 PJ4 R2 PJ4 R3

Elb/hr 1.45E+03 1.57E+03 1.42E+03 1,480.000

lb/mmBtuO2 2.34E-01 2.53E-01 2.32E-01 0.240

mg/dscm 2.54E+02 2.78E+02 2.55E+02 262.333

mg/dscm@7%O2 2.72E+02 2.94E+02 2.69E+02 278.333

ppm 1.33E+02 1.45E+02 1.33E+02 137.000

ppm@7%O2 1.42E+02 1.53E+02 1.40E+02 145.000

Location: Stack Platform - OTM - 27/28

Compound: Filterable PM2.5

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 29.6 35.4 39.9 34.967

lb/mmBtuO2 6.73E-03 8.04E-03 9.11E-03 0.008

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 110.9 66 104.6 93.833

lb/mmBtuO2 2.52E-02 1.50E-02 2.39E-02 0.021

Compound: Organic Condensible Particulate

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 2 1.8 0.7 1.500

lb/mmBtuO2 4.55E-04 4.09E-04 1.60E-04 0.000

Compound: Total PM2.5

Average

RunNumber PJ4 R1 PJ4 R2 PJ4 R3

Mass_mg 142.5 103.2 145.2 130.300

lb/mmBtuO2 3.24E-02 2.35E-02 3.32E-02 0.030

Monday, February 28, 2011 Page 17 of 28
Port Jefferson Unit 4 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 18 of 28
Port Jefferson Unit 4 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 19 of 28
Port Jefferson Unit 4 ICR Test Program

Sampling / Stack Data Results Detail

Location Stack Platform - Method 0011

Average

Run Number PJ4 R1 PJ4 R2 PJ4 R3

Test Date 7/15/2010 7/15/2010 7/15/2010

Run Start Time 7/15/2010 

8:20:00 AM

7/15/2010 

11:10:00 AM

7/15/2010 

1:50:00 PM

Run Finish Time 7/15/2010 

10:36:00 AM

7/15/2010 

1:24:00 PM

7/15/2010 

4:02:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 120 120 120

Nozzle Diameter, inches 0.17 0.17 0.17 0.170

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1 1 1 1.000

Barometric Pressure, inches of Mercury 30.3 30.32 30.32 30.313

Average Orifice Meter Differential, inches H2O 1.39 1.39 1.39 1.390

Dry Gas Meter Volume Sampled, cubic feet 80.884 80.193 83.034 81.370

Average Dry Gas Meter Temperature, °F 77.21 77.21 77.21 77.210

Dry Gas Meter Volume Sampled, dscf 80.779 80.141 82.980 81.300

Total Moisture Liquid collected, g 159.5 159.4 160.3 159.733

Volume of Water Vapor, standard cubic feet 7.51 7.50 7.55 7.520

Moisture Content of Stack Gas, % 8.51 8.56 8.34 8.470

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

Dry Mole Fraction 0.9149 0.9144 0.9166 0.915

Carbon Dioxide, % 10.07 10.05 10.02 10.047

Oxygen, % 8.4 8.34 8.31 8.350

Carbon Monoxide & Nitrogen, % 81.53 81.61 81.67 81.603

Fuel Factor 1.24 1.25 1.26

Dry Molecular Weight, lb/lb-Mole 29.95 29.94 29.94 29.943

Wet Molecular weight, lb/lb-Mole 28.93 28.92 28.94 28.930

Flue Gas Static Pressure, inches of H2O 3 3 3 3.000

Absolute Flue Gas Pressure, inches of Mercury 30.52 30.54 30.54 30.533

Average Stack Gas Temperature, °F 305.00 305.00 305.00 305.000

Average Velocity Head, inches of H2O 2.6896689212

6179

2.689668921

26179

2.689668921

26179

2.690

Average Stack Gas Velocity, feet/second 109.62 109.61 109.57 109.600

Stack Cross-Sectional Area, square feet 346.361 346.361 346.361 346.361

Dry Volumetric Flow Rate, dry scfm 1,467,368.1 1,467,393.4 1,470,387.1 1,468,382.8

67

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,278,085.6 2,277,877.8 2,277,046.5 2,277,669.9

67

Percent Isokinetic of Sampling Rate, % 100.8 100.0 103.3 101.367

Percent Excess Air, % 64.0 63.2 62.7 63.300

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

Round Duct Diameter, inches 252 252 252

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 252 252 252

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 28, 2011 Page 20 of 28
Port Jefferson Unit 4 ICR Test Program

Location Stack Platform - Method 10

Average

Run Number PJ4 R1 PJ4 R2 PJ4 R3

Test Date 7/12/2010 7/13/2010 7/14/2010

Run Start Time 8:10:00 AM 8:00:00 AM 7:50:00 AM

Run Finish Time 4:30:00 PM 4:04:00 PM 4:14:00 PM

Carbon Dioxide, % 10.38 10.26 10.2 10.280

Oxygen, % 7.8 7.94 8.13 7.957

Fuel Factor 1.26 1.26 1.25

Dry Volumetric Flow Rate, dry scfm 1461270.4 1451609.6 1467890.8 1,460,256.9

33

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

Moisture, % 8.73 9.14 9.14 9.003

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 0 174.7 174.7 116.467

Operating Units ppm ppm

No. Readings/Avg. 0 6 6 4.000

Calibration Set 4 3 3 3.333

Calibration Pre Zero Cylinder ID SG9146979 

blank

SG9146979 

blank

SG9146979 

blank

Calibration Pre Zero Cylinder Instrument Response 0 0 0 0.000

Calibration Pre Zero Cylinder Bias 0 0 0 0.000

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID eb0019899 CC210517 CC210517

Calibration Pre High Cylinder Instrument Response 17.3 174.6 173.7 121.867

Calibration Pre High Cylinder Bias 0 -0.23 -0.74 -0.323

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID SG9146979 

blank

SG9146979 

blank

SG9146979 

blank

Calibration Post Zero Cylinder Instrument Response 0 0 0 0.000

Calibration Post Zero Cylinder Bias 0 0 0 0.000

Calibration Post Zero Cylinder Drift 0 0 0 0.000

Calibration Post High Cylinder ID eb0019899 CC210517 CC210517

Calibration Post High Cylinder Instrument Response 17.3 174.6 173.7 121.867

Calibration Post High Cylinder Bias 0 -0.23 -0.74 -0.323

Calibration Post High Cylinder Drift 0 0 0 0.000

Cavg 0.4 0.7 0.6 0.567

Cavg Units ppmvd ppmvd ppmvd

Cgas 0.4023 0.7004 0.6035 0.569

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Cgasw 0 0 0 0.000

Cgasw Units

Monday, February 28, 2011 Page 21 of 28
Port Jefferson Unit 4 ICR Test Program

Location Stack Platform - Method 23

Average

Run Number PJ4 R1 PJ4 R2 PJ4 R3

Test Date 7/12/2010 7/13/2010 7/14/2010

Run Start Time 7/12/2010 

8:10:00 AM

7/13/2010 

8:00:00 AM

7/14/2010 

7:50:00 AM

Run Finish Time 7/12/2010 

4:30:00 PM

7/13/2010 

4:04:00 PM

7/14/2010 

4:14:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 480 480 480

Nozzle Diameter, inches 0.17 0.17 0.17 0.170

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.03 1.03 1.03 1.030

Barometric Pressure, inches of Mercury 30.21 30.25 30.2 30.220

Average Orifice Meter Differential, inches H2O 1.31 1.31 1.31 1.310

Dry Gas Meter Volume Sampled, cubic feet 309.966 310.530 309.660 310.052

Average Dry Gas Meter Temperature, °F 89.75 89.75 89.75 89.750

Dry Gas Meter Volume Sampled, dscf 310.593 311.569 310.184 310.782

Total Moisture Liquid collected, g 631 665.9 667.7 654.867

Volume of Water Vapor, standard cubic feet 29.70 31.34 31.43 30.823

Moisture Content of Stack Gas, % 8.73 9.14 9.20 9.023

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

Dry Mole Fraction 0.9127 0.9086 0.908 0.910

Carbon Dioxide, % 10.38 10.26 10.2 10.280

Oxygen, % 7.8 7.94 8.13 7.957

Carbon Monoxide & Nitrogen, % 81.82 81.8 81.67 81.763

Fuel Factor 1.26 1.26 1.25

Dry Molecular Weight, lb/lb-Mole 29.97 29.96 29.96 29.963

Wet Molecular weight, lb/lb-Mole 28.93 28.87 28.86 28.887

Flue Gas Static Pressure, inches of H2O 3 3 3 3.000

Absolute Flue Gas Pressure, inches of Mercury 30.43 30.47 30.42 30.440

Average Stack Gas Temperature, °F 307.17 307.17 307.17 307.170

Average Velocity Head, inches of H2O 2.6973614709

0879

2.697361470

90879

2.697361470

90879

2.697

Average Stack Gas Velocity, feet/second 110.10 110.14 110.25 110.163

Stack Cross-Sectional Area, square feet 346.361 346.361 346.361 346.361

Dry Volumetric Flow Rate, dry scfm 1,461,767.4 1,457,643.1 1,455,742.7 1,458,384.4

00

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,288,060.8 2,288,892.0 2,291,178.0 2,289,376.9

33

Percent Isokinetic of Sampling Rate, % 97.3 97.9 97.5 97.567

Percent Excess Air, % 56.5 58.1 60.5 58.367

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

Round Duct Diameter, inches 252 252 252

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 252 252 252

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 28, 2011 Page 22 of 28
Port Jefferson Unit 4 ICR Test Program

Location Stack Platform - Method 25A

Average

Run Number PJ4 R1 PJ4 R2 PJ4 R3

Test Date 7/15/2010 7/15/2010 7/15/2010

Run Start Time 8:20:00 AM 11:10:00 AM 1:50:00 PM

Run Finish Time 10:36:00 AM 1:24:00 PM 4:02:00 PM

Carbon Dioxide, % 10.04 10.05 10.02 10.037

Oxygen, % 8.4 8.34 8.31 8.350

Fuel Factor 1.25 1.25 1.26

Dry Volumetric Flow Rate, dry scfm 1466967.4 1472996.6 1478011.5 1,472,658.5

00

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

Moisture, % 8.5 8.64 8.5 8.547

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 17.4 17.4 17 17.267

Operating Units ppm ppm ppm

No. Readings/Avg. 6 6 6 6.000

Calibration Set 4 4 4 4.000

Calibration Pre Zero Cylinder ID SG9146979 

blank

SG9146979 

blank

SG9146979 

blank

Calibration Pre Zero Cylinder Instrument Response 0 0 0 0.000

Calibration Pre Zero Cylinder Bias 0 0 0 0.000

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID eb0019899 eb0019899 eb0019899

Calibration Pre High Cylinder Instrument Response 17.4 17.4 17.4 17.400

Calibration Pre High Cylinder Bias 0.57 0.57 0.57 0.570

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID SG9146979 

blank

SG9146979 

blank

SG9146979 

blank

Calibration Post Zero Cylinder Instrument Response 0 0 0 0.000

Calibration Post Zero Cylinder Bias 0 0 0 0.000

Calibration Post Zero Cylinder Drift 0 0 0 0.000

Calibration Post High Cylinder ID eb0019899 eb0019899 eb0019899

Calibration Post High Cylinder Instrument Response 17.4 17.4 17.4 17.400

Calibration Post High Cylinder Bias 0.57 0.57 0.57 0.570

Calibration Post High Cylinder Drift 0 0 0 0.000

Cavg 0.3 0.7 0.2 0.400

Cavg Units ppmvd ppmvd ppmvd

Cgas 0.3 0.7 0.2 0.400

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Cgasw 0 0 0 0.000

Cgasw Units

Monday, February 28, 2011 Page 23 of 28
Port Jefferson Unit 4 ICR Test Program

Location Stack Platform - Method 26A

Average

Run Number PJ4 R1 PJ4 R2 PJ4 R3

Test Date 7/12/2010 7/12/2010 7/12/2010

Run Start Time 7/12/2010 

8:10:00 AM

7/12/2010 

12:13:00 PM

7/12/2010 

4:00:00 PM

Run Finish Time 7/12/2010 

11:31:00 AM

7/12/2010 

3:34:00 PM

7/12/2010 

7:15:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 180 180 180

Nozzle Diameter, inches 0.17 0.17 0.17 0.170

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.99 0.99 0.99 0.990

Barometric Pressure, inches of Mercury 30.21 30.44 30.2 30.283

Average Orifice Meter Differential, inches H2O 1.64 1.59 1.57 1.600

Dry Gas Meter Volume Sampled, cubic feet 130.215 128.395 126.993 128.534

Average Dry Gas Meter Temperature, °F 85.58 89.17 84.50 86.417

Dry Gas Meter Volume Sampled, dscf 126.471 124.813 123.525 124.936

Total Moisture Liquid collected, g 265.9 239.4 245.2 250.167

Volume of Water Vapor, standard cubic feet 12.52 11.27 11.54 11.777

Moisture Content of Stack Gas, % 9.01 8.28 8.54 8.610

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

Dry Mole Fraction 0.9099 0.9172 0.9146 0.914

Carbon Dioxide, % 10.27 10.51 10.35 10.377

Oxygen, % 7.9 7.75 7.74 7.797

Carbon Monoxide & Nitrogen, % 81.83 81.74 81.91 81.827

Fuel Factor 1.27 1.25 1.27

Dry Molecular Weight, lb/lb-Mole 29.96 29.99 29.97 29.973

Wet Molecular weight, lb/lb-Mole 28.88 29.00 28.95 28.943

Flue Gas Static Pressure, inches of H2O 3 3 3 3.000

Absolute Flue Gas Pressure, inches of Mercury 30.43 30.66 30.42 30.503

Average Stack Gas Temperature, °F 304.25 309.50 308.33 307.360

Average Velocity Head, inches of H2O 2.9453546236

1192

2.846456441

29288

2.812019755

15565

2.868

Average Stack Gas Velocity, feet/second 114.93 112.71 112.48 113.373

Stack Cross-Sectional Area, square feet 346.361 346.361 346.361 346.361

Dry Volumetric Flow Rate, dry scfm 1,527,025.0 1,510,576.0 1,493,724.5 1,510,441.8

33

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,388,436.2 2,342,300.9 2,337,521.1 2,356,086.0

67

Percent Isokinetic of Sampling Rate, % 101.1 100.9 101.0 101.000

Percent Excess Air, % 57.7 56.0 55.7 56.467

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

Round Duct Diameter, inches 252 252 252

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 252 252 252

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 28, 2011 Page 24 of 28
Port Jefferson Unit 4 ICR Test Program

Location Stack Platform - Method 29 

Average

Run Number PJ4 R1 PJ4 R2 PJ4 R3

Test Date 7/13/2010 7/14/2010 7/14/2010

Run Start Time 7/13/2010 

8:00:00 AM

7/14/2010 

7:50:00 AM

7/14/2010 

3:50:00 PM

Run Finish Time 7/13/2010 

2:12:00 PM

7/14/2010 

2:22:00 PM

7/14/2010 

10:15:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 360 360 360

Nozzle Diameter, inches 0.17 0.17 0.17 0.170

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1 1 1 1.000

Barometric Pressure, inches of Mercury 30.25 30.2 30.23 30.227

Average Orifice Meter Differential, inches H2O 1.43 1.43 1.46 1.440

Dry Gas Meter Volume Sampled, cubic feet 248.284 248.951 250.721 249.319

Average Dry Gas Meter Temperature, °F 90.25 90.25 83.42 87.973

Dry Gas Meter Volume Sampled, dscf 241.709 241.959 247.005 243.558

Total Moisture Liquid collected, g 518.7 548.1 541.9 536.233

Volume of Water Vapor, standard cubic feet 24.42 25.80 25.51 25.243

Moisture Content of Stack Gas, % 9.18 9.64 9.36 9.393

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

Dry Mole Fraction 0.9082 0.9036 0.9064 0.906

Carbon Dioxide, % 10.25 10.23 10.17 10.217

Oxygen, % 7.96 8.11 8.15 8.073

Carbon Monoxide & Nitrogen, % 81.79 81.66 81.68 81.710

Fuel Factor 1.26 1.25 1.25

Dry Molecular Weight, lb/lb-Mole 29.96 29.96 29.95 29.957

Wet Molecular weight, lb/lb-Mole 28.86 28.81 28.83 28.833

Flue Gas Static Pressure, inches of H2O 3 3 3 3.000

Absolute Flue Gas Pressure, inches of Mercury 30.47 30.42 30.45 30.447

Average Stack Gas Temperature, °F 310.50 310.50 312.17 311.057

Average Velocity Head, inches of H2O 2.7015451748

8815

2.701545174

88815

2.777870155

94644

2.727

Average Stack Gas Velocity, feet/second 110.48 110.67 112.25 111.133

Stack Cross-Sectional Area, square feet 346.361 346.361 346.361 346.361

Dry Volumetric Flow Rate, dry scfm 1,455,182.8 1,447,922.3 1,471,408.3 1,458,171.1

33

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,295,957.8 2,299,906.3 2,332,741.3 2,309,535.1

33

Percent Isokinetic of Sampling Rate, % 101.4 102.0 102.5 101.967

Percent Excess Air, % 58.4 60.3 60.8 59.833

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

Round Duct Diameter, inches 252 252 252

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 252 252 252

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 28, 2011 Page 25 of 28
Port Jefferson Unit 4 ICR Test Program

Location Stack Platform - Method 6C

Average

Run Number PJ4 R1 PJ4 R2 PJ4 R3

Test Date 7/12/2010 7/12/2010 7/12/2010

Run Start Time 8:10:00 AM 12:13:00 PM 4:00:00 PM

Run Finish Time 11:31:00 AM 3:34:00 PM 7:15:00 PM

Carbon Dioxide, % 10.27 10.51 10.35 10.377

Oxygen, % 7.9 7.75 7.74 7.797

Fuel Factor 1.27 1.25 1.27

Dry Volumetric Flow Rate, dry scfm 1526487.8 1503903.7 1493267.3 1,507,886.2

67

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

Moisture, % 9.01 8.34 8.55 8.633

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 443 443 443 443.000

Operating Units ppm ppm ppm

No. Readings/Avg. 6 6 6 6.000

Calibration Set 2 2 2 2.000

Calibration Pre Zero Cylinder ID SG9146979 

blank

SG9146979 

blank

SG9146979 

blank

Calibration Pre Zero Cylinder Instrument Response 0 0 0 0.000

Calibration Pre Zero Cylinder Bias 0 0 0 0.000

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID cc231248 cc231248 cc231248

Calibration Pre High Cylinder Instrument Response 443.1 443.1 443.1 443.100

Calibration Pre High Cylinder Bias -0.2 -0.2 -0.2 -0.200

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID SG9146979 

blank

SG9146979 

blank

SG9146979 

blank

Calibration Post Zero Cylinder Instrument Response 0 0 0 0.000

Calibration Post Zero Cylinder Bias 0 0 0 0.000

Calibration Post Zero Cylinder Drift 0 0 0 0.000

Calibration Post High Cylinder ID cc231248 cc231248 cc231248

Calibration Post High Cylinder Instrument Response 443.1 443.1 443.1 443.100

Calibration Post High Cylinder Bias -0.2 -0.2 -0.2 -0.200

Calibration Post High Cylinder Drift 0 0 0 0.000

Cavg 258 271.8 274.6 268.133

Cavg Units ppmvd ppmvd ppmvd

Cgas 257.9418 271.7387 274.538 268.073

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Cgasw 0 0 0 0.000

Cgasw Units

Monday, February 28, 2011 Page 26 of 28
Port Jefferson Unit 4 ICR Test Program

Location Stack Platform - Method 7E

Average

Run Number PJ4 R1 PJ4 R2 PJ4 R3

Test Date 7/12/2010 7/12/2010 7/12/2010

Run Start Time 8:10:00 AM 12:13:00 PM 4:00:00 PM

Run Finish Time 11:31:00 AM 3:34:00 PM 7:15:00 PM

Carbon Dioxide, % 10.27 10.51 10.35 10.377

Oxygen, % 7.9 7.75 7.74 7.797

Fuel Factor 1.27 1.25 1.27

Dry Volumetric Flow Rate, dry scfm 1526487.8 1503903.7 1493267 1,507,886.1

67

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

Moisture, % 9.01 8.34 8.55 8.633

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 246 246 246 246.000

Operating Units ppm ppm ppm

No. Readings/Avg. 6 6 6 6.000

Calibration Set 1 1 1 1.000

Calibration Pre Zero Cylinder ID SG9146979 

blank

SG9146979 

blank

SG9146979 

blank

Calibration Pre Zero Cylinder Instrument Response 0 0 0 0.000

Calibration Pre Zero Cylinder Bias 0 0 0 0.000

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC-17285 CC-17285 CC-17285

Calibration Pre High Cylinder Instrument Response 246.6 246.7 246.7 246.667

Calibration Pre High Cylinder Bias -0.57 -0.53 -0.53 -0.543

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID SG9146979 

blank

SG9146979 

blank

SG9146979 

blank

Calibration Post Zero Cylinder Instrument Response 0 0 0 0.000

Calibration Post Zero Cylinder Bias 0 0 0 0.000

Calibration Post Zero Cylinder Drift 0 0 0 0.000

Calibration Post High Cylinder ID CC-17285 CC-17285 CC-17285

Calibration Post High Cylinder Instrument Response 246.6 246.7 246.7 246.667

Calibration Post High Cylinder Bias -0.57 -0.53 -0.53 -0.543

Calibration Post High Cylinder Drift 0 0 0 0.000

Cavg 132.6 145.3 133.1 137.000

Cavg Units ppmvd ppmvd ppmvd

Cgas 132.7075 145.3589 133.154 137.073

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Cgasw 0 0 0 0.000

Cgasw Units

Monday, February 28, 2011 Page 27 of 28
Port Jefferson Unit 4 ICR Test Program

Location Stack Platform - OTM - 27/28

Average

Run Number PJ4 R1 PJ4 R2 PJ4 R3

Test Date 7/13/2010 7/14/2010 7/14/2010

Run Start Time 7/13/2010 

8:00:00 AM

7/14/2010 

7:50:00 AM

7/14/2010 

3:50:00 PM

Run Finish Time 7/13/2010 

2:15:00 PM

7/14/2010 

2:22:00 PM

7/14/2010 

10:15:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 359.08 365.41 360.66

Nozzle Diameter, inches 0.13 0.13 0.13 0.130

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.99 0.99 0.99 0.990

Barometric Pressure, inches of Mercury 30.25 30.2 30.23 30.227

Average Orifice Meter Differential, inches H2O 0.57 0.57 0.57 0.570

Dry Gas Meter Volume Sampled, cubic feet 148.259 150.850 149.642 149.584

Average Dry Gas Meter Temperature, °F 85.33 85.33 86.08 85.580

Dry Gas Meter Volume Sampled, dscf 143.878 146.151 144.925 144.985

Total Moisture Liquid collected, g 284.4 302.5 308.4 298.433

Volume of Water Vapor, standard cubic feet 13.39 14.24 14.52 14.050

Moisture Content of Stack Gas, % 8.51 8.88 9.11 8.833

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

Dry Mole Fraction 0.9149 0.9112 0.9089 0.912

Carbon Dioxide, % 30.25 10.17 10.23 16.883

Oxygen, % 7.96 8.15 8.11 8.073

Carbon Monoxide & Nitrogen, % 61.79 81.68 81.66 75.043

Fuel Factor 0.43 1.25 1.25

Dry Molecular Weight, lb/lb-Mole 33.16 29.95 29.96 31.023

Wet Molecular weight, lb/lb-Mole 31.87 28.89 28.87 29.877

Flue Gas Static Pressure, inches of H2O 3 3 3 3.000

Absolute Flue Gas Pressure, inches of Mercury 30.47 30.42 30.45 30.447

Average Stack Gas Temperature, °F 307.75 307.75 309.83 308.443

Average Velocity Head, inches of H2O 2.6830322743

079

2.683032274

3079

2.715914745

353

2.694

Average Stack Gas Velocity, feet/second 104.59 109.94 110.75 108.427

Stack Cross-Sectional Area, square feet 346.361 346.361 346.361 346.361

Dry Volumetric Flow Rate, dry scfm 1,392,736.6 1,455,664.9 1,460,174.9 1,436,192.1

33

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,173,553.8 2,284,735.7 2,301,568.8 2,253,286.1

00

Percent Isokinetic of Sampling Rate, % 108.1 103.2 103.4 104.900

Percent Excess Air, % 95.3 60.8 60.3 72.133

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

Round Duct Diameter, inches 252 252 252

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 252 252 252

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 28, 2011 Page 28 of 28