Name: Steven Wong

Title: Section Manager

Company: Consolidated Edison Company

Sign Date: 8/24/2010

Name: Mark Looney

Title: President

Company: Environmental Source Samplers, Inc

Sign Date: 8/24/2010

Permitted Facility Representative / Date Testing Company Representative / Date

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.

Saturday, January 29, 2011 Page 1 of 31
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Facility Information:

EAST RIVER GENERATING STATION

801 E. 14th St

New York NY 10009

Contact: Steven Wong

Phone: 212-460-5577

Fax:

Email: wongs@coned.com

Testing Company:

Environmental Source Samplers, Inc

436 Raleigh Street

Wilmington NC 28412

Contact:Mark Looney

Phone: 910-799-1055

Fax: 910-799-1056

Email: mark@essknowsair.com

Air Permit Number: Permitted Source ID/Name:

6

Permitted Maximum Process Rate: Max. Normal Operation Process Rate: Target Process Test Rate

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

 process flow diagram:

Con Edison operates an oil and/or gas fired boiler at the East River Generating Station. East River Unit 6 has a 

dedicated stack which has four 6" diameter test ports, 90 degrees apart. The inside diameter of the stack at the test 

port elevation is 22'-0" but at the top of the stack (56' above the test port elevation), there's a venturi nozzle section 

that tapers parabolically from 22'-0" to 15'-0" diameter. The test ports are just 6", 150# flanges attached on a stub of 

pipe that penetrates into the stack, and there's a platform around the stack at the test port elevation which is about 2.5' 

wide

Industry/SCC/NAIS

Sampling Location Information:

Test Parameter Information:

AFS #: FRS #:

SCC / Description 10100401 External Combustion Boilers - Electric Generation - Residual Oil - Grade 6 Oil: 

Normal 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

UNIT 6 264 0 0 0 672 0 4 6

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

UNIT 6 Carbon Monoxide Method 10 3 240 0

UNIT 6 2,3,7,8-TCDD Method 23 3 480 0

UNIT 6 1,2,3,7,8-PeCDD Method 23 3 480 0

UNIT 6 1,2,3,4,7,8-HxCDD Method 23 3 480 0

UNIT 6 1,2,3,6,7,8-HxCDD Method 23 3 480 0

Saturday, January 29, 2011 Page 2 of 31
8/24/2010

UNIT 6 1,2,3,7,8,9-HxCDD Method 23 3 480 0

UNIT 6 1,2,3,4,6,7,8-HpCDD Method 23 3 480 0

UNIT 6 OCDD Method 23 3 480 0

UNIT 6 2,3,7,8-TCDF Method 23 3 480 0

UNIT 6 1,2,3,7,8-PeCDF Method 23 3 480 0

UNIT 6 2,3,4,7,8-PeCDF Method 23 3 480 0

UNIT 6 1,2,3,4,7,8-HxCDF Method 23 3 480 0

UNIT 6 1,2,3,6,7,8-HxCDF Method 23 3 480 0

UNIT 6 2,3,4,6,7,8-HxCDF Method 23 3 480 0

UNIT 6 1,2,3,7,8,9-HxCDF Method 23 3 480 0

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

UNIT 6 1,2,3,4,7,8,9-HpCDF Method 23 3 480 0

UNIT 6 OCDF Method 23 3 480 0

UNIT 6 Other TCDD Method 23 3 480 0

UNIT 6 Other PeCDD Method 23 3 480 0

UNIT 6 Other HxCDD Method 23 3 480 0

UNIT 6 Other HpCDD Method 23 3 480 0

UNIT 6 Other TCDF Method 23 3 480 0

UNIT 6 Other PeCDF Method 23 3 480 0

UNIT 6 Other HxCDF Method 23 3 480 0

UNIT 6 Other HpCDF Method 23 3 480 0

UNIT 6 Total Dioxins Method 23 3 480 0

UNIT 6 Total Furans Method 23 3 480 0

UNIT 6 3,3',4,4'-TCB (PCB77) Method 23 3 480 0

UNIT 6 3,4,4',5-TCB (PCB81) Method 23 3 480 0

UNIT 6 2,3,3',4,4'-PeCB (PCB105) Method 23 3 480 0

UNIT 6 2,3,4,4',5-PeCB (PCB114) Method 23 3 480 0

UNIT 6 2,3',4,4',5-PeCB (PCB118) Method 23 3 480 0

UNIT 6 2',3,4,4',5-PeCB (PCB123) Method 23 3 480 0

UNIT 6 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)

UNIT 6 Method 23 3 480 0

UNIT 6 2,3',4,4',5,5'-HxCB (PCB167) Method 23 3 480 0

UNIT 6 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 480 0

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

(PCB189)

UNIT 6 Method 23 3 480 0

UNIT 6 Total PCBs Method 23 3 480 0

UNIT 6 Total TEQ Method 23 3 480 0

Total organic compounds 

(TOC) as Propane

UNIT 6 Method 25A 3 180 0

UNIT 6 Filterable PM2.5 OTM - 27/28 3 240 0

UNIT 6 Filterable Particulate OTM - 27/28 3 240 0

Organic Condensible 

Particulate

UNIT 6 OTM - 27/28 3 240 0

UNIT 6 Total Particulate OTM - 27/28 3 240 0

UNIT 6 Filterable PM2.5 - PM10 OTM - 27/28 3 240 0

UNIT 6 Total PM2.5 OTM - 27/28 3 240 0

Inorganic (Aqueous) 

Condensible Part.

UNIT 6 OTM - 27/28 3 240 0

UNIT 6 Filterable PM10 OTM - 27/28 3 240 0

UNIT 6 Nickel Method 29 3 240 0

UNIT 6 Mercury Method 29 3 240 0

UNIT 6 Antimony Method 29 3 240 0

Saturday, January 29, 2011 Page 3 of 31
8/24/2010

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

UNIT 6 Arsenic Method 29 3 240 0

UNIT 6 Beryllium Method 29 3 240 0

UNIT 6 Cadmium Method 29 3 240 0

UNIT 6 Chromium Method 29 3 240 0

UNIT 6 Magnesium Method 29 3 240 0

UNIT 6 Selenium Method 29 3 240 0

UNIT 6 Lead Method 29 3 240 0

UNIT 6 O2 Method 3A O2 3 240 0

UNIT 6 Co2 Method 3A CO2 3 240 0

UNIT 6 Sulfur Dioxide Method 6C 3 240 0

UNIT 6 Nitrogen oxides (NOx) Method 7E 3 240 0

Saturday, January 29, 2011 Page 4 of 31
8/24/2010

Sampling / Stack Data Results Summary

Location UNIT 6 - Method 10

Average

Run Number 1 2 3

Test Date 4/29/2010 4/29/2010 4/29/2010

Run Start Time 8:15:00 AM 11:31:00 

AM

3:00:00 PM

Run Finish Time 11:14:00 AM 2:30:00 PM 5:59:00 PM

Carbon Dioxide, % 10.426 10.4267 10.53 10.461

Oxygen, % 10.045 9.8808 9.8194 9.915

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Location UNIT 6 - Method 23

Average

Run Number 1 2 3

Test Date 4/27/2010 4/28/2010 4/29/2010

Run Start Time 8:30:00 AM 10:50:00 

AM

11:31:00 AM

Run Finish Time 4:05:00 PM 7:25:00 PM 8:09:00 PM

Net Run Time, minutes 480 480 480

Dry Gas Meter Volume Sampled, dscf 326.645 329.212 332.647 329.501

Moisture Content of Stack Gas, % 7.51 7.30 7.38 7.397

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

Carbon Dioxide, % 10.04 10.55 10.46 10.350

Oxygen, % 10.17 10.19 9.92 10.093

Average Stack Gas Temperature, °F 300.34 302.71 306.30 303.117

Dry Volumetric Flow Rate, dry scfm 314,076.6 311,385.8 311,718.6 312,393.667

Actual Wet Volumetric Flue Gas Flow Rate, acfm 493,792.8 491,968.1 491,740.0 492,500.300

Percent Isokinetic of Sampling Rate, % 104.6 106.3 107.3 106.067

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

Saturday, January 29, 2011 Page 5 of 31
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Location UNIT 6 - Method 25A

Average

Run Number 1 2 3

Test Date 4/29/2010 4/29/2010 4/29/2010

Run Start Time 8:15:00 AM 11:31:00 

AM

3:00:00 PM

Run Finish Time 11:14:00 AM 2:30:00 PM 5:59:00 PM

Carbon Dioxide, % 10.4264 10.4267 10.53 10.461

Oxygen, % 10.0484 9.8808 9.8194 9.916

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Location UNIT 6 - Method 29

Average

Run Number 1 2 3

Test Date 4/28/2010 4/28/2010 4/29/2010

Run Start Time 12:30:00 PM 5:15:00 PM 8:15:00 AM

Run Finish Time 4:55:00 PM 9:35:00 PM 12:35:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 168.476 152.689 158.650 159.938

Moisture Content of Stack Gas, % 7.22 7.40 7.41 7.343

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

Carbon Dioxide, % 10.49 10.74 10.4264 10.552

Oxygen, % 10.28 10.07 10.0484 10.133

Average Stack Gas Temperature, °F 302.08 302.00 302.46 302.180

Dry Volumetric Flow Rate, dry scfm 307,203.7 312,783.1 310,862.8 310,283.200

Actual Wet Volumetric Flue Gas Flow Rate, acfm 484,213.4 494,248.9 488,090.8 488,851.033

Percent Isokinetic of Sampling Rate, % 99.5 88.6 92.6 93.567

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

Saturday, January 29, 2011 Page 6 of 31
8/24/2010

Location UNIT 6 - Method 3A CO2

Average

Run Number 1 2 3

Test Date 4/29/2010 4/29/2010 4/29/2010

Run Start Time 8:15:00 AM 11:31:00 

AM

3:00:00 PM

Run Finish Time 11:14:00 AM 2:30:00 PM 5:59:00 PM

Carbon Dioxide, % 10.426 10.427 10.53 10.461

Oxygen, % 10.0484 9.8808 9.8194 9.916

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Location UNIT 6 - Method 3A CO2 3

Average

Run Number 4

Test Date 4/29/2010

Run Start Time 6:10:00 PM

Run Finish Time 8:09:00 PM

Carbon Dioxide, % 10.838 10.838

Oxygen, % 9.8876 9.888

Dry Volumetric Flow Rate, dry scfm 0 0.000

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

Moisture, % 0 0.000

Fuel Type Oil

Fw 10320 10,320.000

Fc 1420 1,420.000

Saturday, January 29, 2011 Page 7 of 31
8/24/2010

Location UNIT 6 - Method 3A O2

Average

Run Number 1 2 3

Test Date 4/29/2010 4/29/2010 4/29/2010

Run Start Time 8:15:00 AM 11:31:00 

AM

3:00:00 PM

Run Finish Time 11:14:00 AM 2:30:00 PM 5:59:00 PM

Carbon Dioxide, % 10.426 10.427 10.53 10.461

Oxygen, % 10.0484 9.8808 9.8194 9.916

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Location UNIT 6 - Method 3A O2 3

Average

Run Number 4

Test Date 4/29/2010

Run Start Time 6:10:00 PM

Run Finish Time 8:09:00 PM

Carbon Dioxide, % 10.838 10.838

Oxygen, % 9.8876 9.888

Dry Volumetric Flow Rate, dry scfm 0 0.000

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

Moisture, % 0 0.000

Fuel Type Oil

Fw 10320 10,320.000

Fc 1420 1,420.000

Saturday, January 29, 2011 Page 8 of 31
8/24/2010

Location UNIT 6 - Method 6C

Average

Run Number 1 2 3

Test Date 4/29/2010 4/29/2010 4/29/2010

Run Start Time 8:15:00 AM 11:31:00 

AM

3:00:00 PM

Run Finish Time 11:14:00 AM 2:30:00 PM 5:59:00 PM

Carbon Dioxide, % 10.4264 10.4267 10.53 10.461

Oxygen, % 10.0484 9.8808 9.8194 9.916

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Location UNIT 6 - OTM - 27/28

Average

Run Number 1 2 3

Test Date 4/28/2010 4/28/2010 4/29/2010

Run Start Time 7:20:00 AM 12:30:00 

PM

5:15:00 PM

Run Finish Time 11:45:00 AM 4:55:00 PM 9:35:00 PM

Net Run Time, minutes 244.5 247.5 239.5

Dry Gas Meter Volume Sampled, dscf 91.311 93.442 89.854 91.536

Moisture Content of Stack Gas, % 7.26 6.59 6.83 6.893

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

Carbon Dioxide, % 12.75 12.75 12.75 12.750

Oxygen, % 7 7 7 7.000

Average Stack Gas Temperature, °F 302.25 303.25 303.71 303.070

Dry Volumetric Flow Rate, dry scfm 313,424.2 318,541.5 308,004.6 313,323.433

Actual Wet Volumetric Flue Gas Flow Rate, acfm 491,512.0 497,442.0 481,704.5 490,219.500

Percent Isokinetic of Sampling Rate, % 81.1 79.7 81.9 80.900

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

Saturday, January 29, 2011 Page 9 of 31
8/24/2010

Emissions Summary

Location: UNIT 6 - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 7.49E-05 1.01E-03 5.15E-04 0.001

ppm 5.82E-02 7.99E-01 4.09E-01 0.422

ppm@7%O2 7.45E-02 1.01E+00 5.13E-01 0.533

Location: UNIT 6 - Method 23

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000917 0.00000000597 0 0.000

lb/mmBtuO2 1.11E-12 7.17E-13 0.00E+00 0.000

ng/dscm 9.92E-04 6.41E-04 0.00E+00 0.001

ng/dscm@7%O2 1.29E-03 8.32E-04 0.00E+00 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000604 0.00000000432 0 0.000

lb/mmBtuO2 7.30E-13 5.19E-13 0.00E+00 0.000

ng/dscm 6.53E-04 4.63E-04 0.00E+00 0.000

ng/dscm@7%O2 8.46E-04 6.01E-04 0.00E+00 0.000

Compound: 1,2,3,4,7,8,9-HpCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000022 0.00000000178 0 0.000

lb/mmBtuO2 2.66E-13 2.14E-13 0.00E+00 0.000

ng/dscm 2.38E-04 1.91E-04 0.00E+00 0.000

ng/dscm@7%O2 3.08E-04 2.48E-04 0.00E+00 0.000

Compound: 1,2,3,4,7,8-HxCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000187 0.00000000168 0 0.000

lb/mmBtuO2 2.26E-13 2.02E-13 0.00E+00 0.000

ng/dscm 2.02E-04 1.80E-04 0.00E+00 0.000

ng/dscm@7%O2 2.62E-04 2.34E-04 0.00E+00 0.000

Compound: 1,2,3,4,7,8-HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000000202 0.00000000232 0 0.000

lb/mmBtuO2 2.44E-13 2.79E-13 0.00E+00 0.000

ng/dscm 2.18E-04 2.49E-04 0.00E+00 0.000

ng/dscm@7%O2 2.82E-04 3.23E-04 0.00E+00 0.000

Compound: 1,2,3,6,7,8-HxCDD

Average

Saturday, January 29, 2011 Page 10 of 31
8/24/2010

RunNumber 1 2 3

Mass_mg 0.00000000195 0.00000000172 0 0.000

lb/mmBtuO2 2.36E-13 2.07E-13 0.00E+00 0.000

ng/dscm 2.11E-04 1.85E-04 0.00E+00 0.000

ng/dscm@7%O2 2.73E-04 2.40E-04 0.00E+00 0.000

Compound: 1,2,3,6,7,8-HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000000208 0.00000000193 0 0.000

lb/mmBtuO2 2.51E-13 2.32E-13 0.00E+00 0.000

ng/dscm 2.25E-04 2.07E-04 0.00E+00 0.000

ng/dscm@7%O2 2.91E-04 2.69E-04 0.00E+00 0.000

Compound: 1,2,3,7,8,9-HxCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000345 0.0000000018 0 0.000

lb/mmBtuO2 4.17E-13 2.16E-13 0.00E+00 0.000

ng/dscm 3.73E-04 1.93E-04 0.00E+00 0.000

ng/dscm@7%O2 4.83E-04 2.50E-04 0.00E+00 0.000

Compound: 1,2,3,7,8,9-HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000000199 0.00000000174 0 0.000

lb/mmBtuO2 2.40E-13 2.09E-13 0.00E+00 0.000

ng/dscm 2.15E-04 1.87E-04 0.00E+00 0.000

ng/dscm@7%O2 2.79E-04 2.43E-04 0.00E+00 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000188 0.00000000212 0 0.000

lb/mmBtuO2 2.27E-13 2.55E-13 0.00E+00 0.000

ng/dscm 2.03E-04 2.27E-04 0.00E+00 0.000

ng/dscm@7%O2 2.63E-04 2.95E-04 0.00E+00 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000013 0.00000000212 0 0.000

lb/mmBtuO2 1.57E-13 2.55E-13 0.00E+00 0.000

ng/dscm 1.41E-04 2.27E-04 0.00E+00 0.000

ng/dscm@7%O2 1.83E-04 2.95E-04 0.00E+00 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000152 0.0000000102 0 0.000

lb/mmBtuO2 1.84E-12 1.22E-12 0.00E+00 0.000

ng/dscm 1.64E-03 1.09E-03 0.00E+00 0.001

ng/dscm@7%O2 2.12E-03 1.41E-03 0.00E+00 0.001

Saturday, January 29, 2011 Page 11 of 31
8/24/2010

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

Average

RunNumber 1 2 3

Mass_mg 0.000000132 0.0000000804 0 0.000

lb/mmBtuO2 1.59E-11 9.66E-12 0.00E+00 0.000

ng/dscm 1.43E-02 8.63E-03 0.00E+00 0.008

ng/dscm@7%O2 1.85E-02 1.12E-02 0.00E+00 0.010

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

Average

RunNumber 1 2 3

Mass_mg 0.000000685 0.000000423 0 0.000

lb/mmBtuO2 8.28E-11 5.08E-11 0.00E+00 0.000

ng/dscm 7.41E-02 4.54E-02 0.00E+00 0.040

ng/dscm@7%O2 9.60E-02 5.89E-02 0.00E+00 0.052

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000503 0.0000000272 0 0.000

lb/mmBtuO2 6.08E-12 3.27E-12 0.00E+00 0.000

ng/dscm 5.44E-03 2.92E-03 0.00E+00 0.003

ng/dscm@7%O2 7.05E-03 3.79E-03 0.00E+00 0.004

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000472 0.0000000328 0 0.000

lb/mmBtuO2 5.70E-12 3.94E-12 0.00E+00 0.000

ng/dscm 5.10E-03 3.52E-03 0.00E+00 0.003

ng/dscm@7%O2 6.61E-03 4.57E-03 0.00E+00 0.004

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

Average

RunNumber 1 2 3

Mass_mg 0.00000184 0.00000121 0 0.000

lb/mmBtuO2 2.22E-10 1.45E-10 0.00E+00 0.000

ng/dscm 1.99E-01 1.30E-01 0.00E+00 0.110

ng/dscm@7%O2 2.58E-01 1.69E-01 0.00E+00 0.142

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000353 0.0000000311 0 0.000

lb/mmBtuO2 4.26E-12 3.74E-12 0.00E+00 0.000

ng/dscm 3.82E-03 3.34E-03 0.00E+00 0.002

ng/dscm@7%O2 4.95E-03 4.33E-03 0.00E+00 0.003

Compound: 2,3,4,6,7,8-HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000000259 0.00000000127 0 0.000

lb/mmBtuO2 3.13E-13 1.53E-13 0.00E+00 0.000

Saturday, January 29, 2011 Page 12 of 31
8/24/2010

ng/dscm 2.80E-04 1.36E-04 0.00E+00 0.000

ng/dscm@7%O2 3.63E-04 1.77E-04 0.00E+00 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000262 0.00000000299 0 0.000

lb/mmBtuO2 3.17E-13 3.59E-13 0.00E+00 0.000

ng/dscm 2.83E-04 3.21E-04 0.00E+00 0.000

ng/dscm@7%O2 3.67E-04 4.17E-04 0.00E+00 0.000

Compound: 2,3,7,8-TCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000153 0.00000000151 0 0.000

lb/mmBtuO2 1.85E-13 1.81E-13 0.00E+00 0.000

ng/dscm 1.65E-04 1.62E-04 0.00E+00 0.000

ng/dscm@7%O2 2.14E-04 2.10E-04 0.00E+00 0.000

Compound: 2,3,7,8-TCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000023 0.00000000429 0 0.000

lb/mmBtuO2 2.78E-13 5.15E-13 0.00E+00 0.000

ng/dscm 2.49E-04 4.60E-04 0.00E+00 0.000

ng/dscm@7%O2 3.23E-04 5.97E-04 0.00E+00 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000266 0.0000000153 0 0.000

lb/mmBtuO2 3.21E-12 1.84E-12 0.00E+00 0.000

ng/dscm 2.88E-03 1.64E-03 0.00E+00 0.002

ng/dscm@7%O2 3.73E-03 2.13E-03 0.00E+00 0.002

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000201 0.0000000128 0 0.000

lb/mmBtuO2 2.43E-12 1.54E-12 0.00E+00 0.000

ng/dscm 2.17E-03 1.37E-03 0.00E+00 0.001

ng/dscm@7%O2 2.81E-03 1.78E-03 0.00E+00 0.002

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

Average

RunNumber 1 2 3

Mass_mg 0.0000003 0.000000181 0 0.000

lb/mmBtuO2 3.62E-11 2.17E-11 0.00E+00 0.000

ng/dscm 3.24E-02 1.94E-02 0.00E+00 0.017

ng/dscm@7%O2 4.20E-02 2.52E-02 0.00E+00 0.022

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

Average

RunNumber 1 2 3

Saturday, January 29, 2011 Page 13 of 31
8/24/2010

Mass_mg 0.0000000175 0.0000000135 0 0.000

lb/mmBtuO2 2.11E-12 1.62E-12 0.00E+00 0.000

ng/dscm 1.89E-03 1.45E-03 0.00E+00 0.001

ng/dscm@7%O2 2.45E-03 1.88E-03 0.00E+00 0.001

Compound: OCDD

Average

RunNumber 1 2 3

Mass_mg 0.000000023 0.0000000102 0 0.000

lb/mmBtuO2 2.78E-12 1.22E-12 0.00E+00 0.000

ng/dscm 2.49E-03 1.09E-03 0.00E+00 0.001

ng/dscm@7%O2 3.23E-03 1.41E-03 0.00E+00 0.002

Compound: OCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000000282 0.00000000334 0 0.000

lb/mmBtuO2 3.41E-13 4.01E-13 0.00E+00 0.000

ng/dscm 3.05E-04 3.58E-04 0.00E+00 0.000

ng/dscm@7%O2 3.95E-04 4.65E-04 0.00E+00 0.000

Compound: Other HpCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000875 0.00000000464 0 0.000

lb/mmBtuO2 1.06E-12 5.57E-13 0.00E+00 0.000

ng/dscm 9.46E-04 4.98E-04 0.00E+00 0.000

ng/dscm@7%O2 1.23E-03 6.46E-04 0.00E+00 0.001

Compound: Other HpCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000000382 0.000000003 0 0.000

lb/mmBtuO2 4.62E-13 3.60E-13 0.00E+00 0.000

ng/dscm 4.13E-04 3.22E-04 0.00E+00 0.000

ng/dscm@7%O2 5.35E-04 4.18E-04 0.00E+00 0.000

Compound: Other HxCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000003242 0.00000002871 0 0.000

lb/mmBtuO2 3.92E-12 3.45E-12 0.00E+00 0.000

ng/dscm 3.51E-03 3.08E-03 0.00E+00 0.002

ng/dscm@7%O2 4.55E-03 4.00E-03 0.00E+00 0.003

Compound: Other HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000002672 0.00000002145 0 0.000

lb/mmBtuO2 3.23E-12 2.58E-12 0.00E+00 0.000

ng/dscm 2.89E-03 2.30E-03 0.00E+00 0.002

ng/dscm@7%O2 3.74E-03 2.99E-03 0.00E+00 0.002

Saturday, January 29, 2011 Page 14 of 31
8/24/2010

Compound: Other PeCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000003635 0.00000003112 0 0.000

lb/mmBtuO2 4.39E-12 3.74E-12 0.00E+00 0.000

ng/dscm 3.93E-03 3.34E-03 0.00E+00 0.002

ng/dscm@7%O2 5.09E-03 4.33E-03 0.00E+00 0.003

Compound: Other PeCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000003351 0.0000000264 0 0.000

lb/mmBtuO2 4.05E-12 3.17E-12 0.00E+00 0.000

ng/dscm 3.62E-03 2.83E-03 0.00E+00 0.002

ng/dscm@7%O2 4.69E-03 3.67E-03 0.00E+00 0.003

Compound: Other TCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000004806 0.00000004736 0 0.000

lb/mmBtuO2 5.81E-12 5.69E-12 0.00E+00 0.000

ng/dscm 5.20E-03 5.08E-03 0.00E+00 0.003

ng/dscm@7%O2 6.74E-03 6.59E-03 0.00E+00 0.004

Compound: Other TCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000004312 0.0000000386 0 0.000

lb/mmBtuO2 5.21E-12 4.64E-12 0.00E+00 0.000

ng/dscm 4.66E-03 4.14E-03 0.00E+00 0.003

ng/dscm@7%O2 6.04E-03 5.37E-03 0.00E+00 0.004

Compound: Total Dioxins

Average

RunNumber 1 2 3

Mass_mg 0.00000008585 0.00000008585 0 0.000

lb/mmBtuO2 1.04E-11 1.03E-11 0.00E+00 0.000

ng/dscm 9.28E-03 9.21E-03 0.00E+00 0.006

ng/dscm@7%O2 1.20E-02 1.20E-02 0.00E+00 0.008

Compound: Total Furans

Average

RunNumber 1 2 3

Mass_mg 0.00000004244 0.00000004244 0 0.000

lb/mmBtuO2 5.13E-12 5.10E-12 0.00E+00 0.000

ng/dscm 4.59E-03 4.55E-03 0.00E+00 0.003

ng/dscm@7%O2 5.95E-03 5.91E-03 0.00E+00 0.004

Compound: Total PCBs

Average

RunNumber 1 2 3

Mass_mg 0.0000030073 0.0000019216 0 0.000

lb/mmBtuO2 3.63E-10 2.31E-10 0.00E+00 0.000

Saturday, January 29, 2011 Page 15 of 31
8/24/2010

ng/dscm 3.25E-01 2.06E-01 0.00E+00 0.177

ng/dscm@7%O2 4.21E-01 2.67E-01 0.00E+00 0.229

Compound: Total TEQ

Average

RunNumber 1 2 3

Mass_mg 0.00000000587 0.00000000598 0 0.000

lb/mmBtuO2 7.09E-13 7.18E-13 0.00E+00 0.000

ng/dscm 6.35E-04 6.42E-04 0.00E+00 0.000

ng/dscm@7%O2 8.23E-04 8.33E-04 0.00E+00 0.001

Location: UNIT 6 - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

Location: UNIT 6 - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.3721 0.4171 0.4161 0.402

lb/mmBtuO2 8.81E-05 1.07E-04 1.02E-04 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.0088 0.0095645 0.009314 0.009

lb/mmBtuO2 2.08E-06 2.45E-06 2.29E-06 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.001615 0.002095 0.002105 0.002

lb/mmBtuO2 3.82E-07 5.36E-07 5.18E-07 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.0052 0.0018505 0.00443 0.004

lb/mmBtuO2 1.23E-06 4.74E-07 1.09E-06 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.00592 0.009295 0.00656 0.007

lb/mmBtuO2 1.40E-06 2.38E-06 1.61E-06 0.000

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.009771 0.013165 0.013229 0.012

lb/mmBtuO2 2.31E-06 3.37E-06 3.25E-06 0.000

Saturday, January 29, 2011 Page 16 of 31
8/24/2010

Compound: Magnesium

Average

RunNumber 1 2 3

Mass_mg 0.30083 0.348555 0.34524 0.332

lb/mmBtuO2 7.12E-05 8.93E-05 8.49E-05 0.000

Compound: Mercury

Average

RunNumber 1 2 3

Mass_mg 0.00113 0.000032 0.00084 0.001

lb/mmBtuO2 2.67E-07 8.19E-09 2.07E-07 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 1.94568 2.226545 2.23911 2.137

lb/mmBtuO2 4.60E-04 5.70E-04 5.51E-04 0.001

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.02206 0.0053635 0.0125 0.013

lb/mmBtuO2 5.22E-06 1.37E-06 3.07E-06 0.000

Location: UNIT 6 - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

lb/mmBtuO2 2.04E-01 2.12E-01 2.25E-01 0.214

ppm 6.92E+01 7.32E+01 7.79E+01 73.433

ppm@7%O2 8.86E+01 9.23E+01 9.77E+01 92.867

Location: UNIT 6 - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 20.2 13.6 21.5 18.433

lb/mmBtuO2 6.74E-03 4.43E-03 7.29E-03 0.006

Compound: Filterable PM10

Average

RunNumber 1 2 3

Mass_mg 3.26 0.23 1.39 1.627

lb/mmBtuO2 1.09E-03 7.50E-05 4.71E-04 0.001

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 16.4 11.8 20 16.067

lb/mmBtuO2 5.47E-03 3.85E-03 6.78E-03 0.005

Saturday, January 29, 2011 Page 17 of 31
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Process Run Data

Compound: Filterable PM2.5 - PM10

Average

RunNumber 1 2 3

Mass_mg 0.46 1.64 0.17 0.757

lb/mmBtuO2 1.53E-04 5.35E-04 5.76E-05 0.000

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 5.7 8.8 9.9 8.133

lb/mmBtuO2 1.90E-03 2.87E-03 3.36E-03 0.003

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 5.7 8.6 10.4 8.233

lb/mmBtuO2 1.90E-03 2.80E-03 3.53E-03 0.003

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 41.4 31.1 41.8 38.100

lb/mmBtuO2 1.38E-02 1.01E-02 1.42E-02 0.013

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 37.6 29.3 40.3 35.733

lb/mmBtuO2 1.25E-02 9.55E-03 1.37E-02 0.012

Saturday, January 29, 2011 Page 18 of 31
8/24/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Natural Gas Flow 69.62 Kscf/hr 0

10 Natural Gas Flow 61.87 Kscf/hr 0

11 Natural Gas Flow 63.5 Kscf/hr 0

12 Natural Gas Flow 65.99 Kscf/hr 0

2 Natural Gas Flow 71.18 Kscf/hr 0

3 Natural Gas Flow 70.04 Kscf/hr 0

4 Natural Gas Flow 73.66 Kscf/hr 0

5 Natural Gas Flow 60.47 Kscf/hr 0

6 Natural Gas Flow 60.16 Kscf/hr 0

7 Natural Gas Flow 62.7 Kscf/hr 0

8 Natural Gas Flow 64.21 Kscf/hr 0

9 Natural Gas Flow 60.77 Kscf/hr 0

1 Unit Gross Electical Output 72.9 MW 0

10 Unit Gross Electical Output 73 MW 0

11 Unit Gross Electical Output 72.9 MW 0

12 Unit Gross Electical Output 72.9 MW 0

2 Unit Gross Electical Output 73.1 MW 0

3 Unit Gross Electical Output 72.8 MW 0

4 Unit Gross Electical Output 72.8 MW 0

5 Unit Gross Electical Output 72.9 MW 0

6 Unit Gross Electical Output 73.1 MW 0

7 Unit Gross Electical Output 73 MW 0

8 Unit Gross Electical Output 73 MW 0

9 Unit Gross Electical Output 73 MW 0

1 Residual Oil (No. 6) Burned 1000 Gallons/million BTU using O2 38.59 0 4/27/2010 Run1

10 Residual Oil (No. 6) Burned 1000 Gallons/million BTU using O2 37.86 0 4/29/2010 Run 2

11 Residual Oil (No. 6) Burned 1000 Gallons/million BTU using O2 38.33 0 4/29/2010 Run 3

12 Residual Oil (No. 6) Burned 1000 Gallons/million BTU using O2 38.22 0 4/29/2010 Run 4

2 Residual Oil (No. 6) Burned 1000 Gallons/million BTU using O2 38.62 0 4/27/2010 Run 2

3 Residual Oil (No. 6) Burned 1000 Gallons/million BTU using O2 38.62 0 4/27/2010 Run 3

4 Residual Oil (No. 6) Burned 1000 Gallons/million BTU using O2 38.65 0 4/27/2010 Run 4

5 Residual Oil (No. 6) Burned 1000 Gallons/million BTU using O2 37.98 0 4/28/2010 Run 1

6 Residual Oil (No. 6) Burned 1000 Gallons/million BTU using O2 37.91 0 4/28/2010 Run 2

Saturday, January 29, 2011 Page 19 of 31
8/24/2010

APCD Run Data

Process Lab Run Data

7 Residual Oil (No. 6) Burned 1000 Gallons/million BTU using O2 37.81 0 4/28/2010 Run 3

8 Residual Oil (No. 6) Burned 1000 Gallons/million BTU using O2 37.81 0 4/28/2010 Run 4

9 Residual Oil (No. 6) Burned 1000 Gallons/million BTU using O2 37.87 0 4/29/2010 Run 1

Run Name Value UOM Comments

Target

Value

1 VENTURI SCRUBBER 0 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value 18849 Btu/lb

2 Fuel Higher Heating Value 18864 Btu/lb

3 Fuel Higher Heating Value 18854 Btu/lb

1 Fuel Mercury Content 0.029 ppm

2 Fuel Mercury Content 0.029 ppm

3 Fuel Mercury Content 0.033 ppm

1 Fuel Cadmium Content 0.51 ppm

2 Fuel Cadmium Content 0.48 ppm

3 Fuel Cadmium Content 0.48 ppm

1 Fuel Nickel Content 8 ppm

2 Fuel Nickel Content 7.5 ppm

3 Fuel Nickel Content 5.6 ppm

1 Fuel Arsenic Content 2 ppm

2 Fuel Arsenic Content 1.9 ppm

3 Fuel Arsenic Content 1.9 ppm

1 Fuel Chromium Content 1 ppm

2 Fuel Chromium Content 0.48 ppm

3 Fuel Chromium Content 0.96 ppm

1 Fuel Beryllium Content 0.2 ppm

2 Fuel Beryllium Content 0.19 ppm

3 Fuel Beryllium Content 0.19 ppm

1 Fuel Lead Content 2 ppm

2 Fuel Lead Content 1.9 ppm

3 Fuel Lead Content 1.9 ppm

1 Fuel Manganese Content 1.8 ppm

2 Fuel Manganese Content 1.4 ppm

3 Fuel Manganese Content 1.4 ppm

1 Fuel Chlorine Content 20 ppm

2 Fuel Chlorine Content 20 ppm

3 Fuel Chlorine Content 20 ppm

1 Fuel Phosphorus Content 3 ppm

Saturday, January 29, 2011 Page 20 of 31
8/24/2010

1 Fuel Selenium Content 2 ppm

1 Fuel Cobalt Content 5.1 ppm

Saturday, January 29, 2011 Page 21 of 31
8/24/2010

Sampling / Stack Data Results Detail

Location UNIT 6 - Method 10

Average

Run Number 1 2 3

Test Date 4/29/2010 4/29/2010 4/29/2010

Run Start Time 8:15:00 AM 11:31:00 AM 3:00:00 PM

Run Finish Time 11:14:00 AM 2:30:00 PM 5:59:00 PM

Carbon Dioxide, % 10.426 10.4267 10.53 10.461

Oxygen, % 10.045 9.8808 9.8194 9.915

Fuel Factor 1.04 1.06 1.05

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 0 0 0 0.000

Operating Units PPM PPM ppm

No. Readings/Avg. 180 180 180 180.000

Calibration Set 3 3 3 3.000

Calibration Pre Zero Cylinder ID CC CC CC

Calibration Pre Zero Cylinder Instrument Response 1.271 -0.4 0.343 0.405

Calibration Pre Zero Cylinder Bias 0.53 -1.28 -0.47 -0.407

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID SG9111990B

AL

SG9111990B

AL

SG9111990B

AL

Calibration Pre High Cylinder Instrument Response 91.6 91.789 91.663 91.684

Calibration Pre High Cylinder Bias -1.17 -0.96 -1.1 -1.077

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC CC CC

Calibration Post Zero Cylinder Instrument Response -0.4 0.343 0.29 0.078

Calibration Post Zero Cylinder Bias -1.28 -0.47 -0.53 -0.760

Calibration Post Zero Cylinder Drift 1.81 0.81 6.000000000

00001E-02

0.893

Calibration Post High Cylinder ID SG9111990B

AL

SG9111990B

AL

SG9111990B

AL

Calibration Post High Cylinder Instrument Response 91.789 91.663 91.05 91.501

Calibration Post High Cylinder Bias -0.96 -1.1 -1.77 -1.277

Calibration Post High Cylinder Drift 0.21 0.14 0.67 0.340

Cavg 0.492 0.751 0.712 0.652

Cavg Units ppmvd ppmvd ppmvd

Cgas 0.0582 0.7991 0.4086 0.422

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

Saturday, January 29, 2011 Page 22 of 31
8/24/2010

Location UNIT 6 - Method 23

Average

Run Number 1 2 3

Test Date 4/27/2010 4/28/2010 4/29/2010

Run Start Time 8:30:00 AM 10:50:00 AM 11:31:00 AM

Run Finish Time 4:05:00 PM 7:25:00 PM 8:09:00 PM

Net Traversing Points 1 1 1

Net Run Time, minutes 480 480 480

Nozzle Diameter, inches 0.38 0.38 0.38 0.380

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9852 0.9852 0.9852 0.985

Barometric Pressure, inches of Mercury 29.642 29.528 29.728 29.633

Average Orifice Meter Differential, inches H2O 1.57 1.57 1.56 1.567

Dry Gas Meter Volume Sampled, cubic feet 334.304 331.782 337.192 334.426

Average Dry Gas Meter Temperature, °F 69.49 59.40 65.93 64.940

Dry Gas Meter Volume Sampled, dscf 326.645 329.212 332.647 329.501

Total Moisture Liquid collected, g 563.4 550.4 562.7 558.833

Volume of Water Vapor, standard cubic feet 26.52 25.91 26.49 26.307

Moisture Content of Stack Gas, % 7.51 7.30 7.38 7.397

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

Dry Mole Fraction 0.9249 0.927 0.9262 0.926

Carbon Dioxide, % 10.04 10.55 10.46 10.350

Oxygen, % 10.17 10.19 9.92 10.093

Carbon Monoxide & Nitrogen, % 79.79 79.26 79.62 79.557

Fuel Factor 1.07 1.02 1.05

Dry Molecular Weight, lb/lb-Mole 30.01 30.10 30.07 30.060

Wet Molecular weight, lb/lb-Mole 29.11 29.22 29.18 29.170

Flue Gas Static Pressure, inches of H2O -0.1 -0.2 -0.15 -0.150

Absolute Flue Gas Pressure, inches of Mercury 29.63 29.51 29.72 29.620

Average Stack Gas Temperature, °F 300.34 302.71 306.30 303.117

Average Velocity Head, inches of H2O 0.1031 0.102 0.102 0.102

Average Stack Gas Velocity, feet/second 21.65 21.57 21.56 21.593

Stack Cross-Sectional Area, square feet 380.133 380.133 380.133 380.133

Dry Volumetric Flow Rate, dry scfm 314,076.6 311,385.8 311,718.6 312,393.667

Actual Wet Volumetric Flue Gas Flow Rate, acfm 493,792.8 491,968.1 491,740.0 492,500.300

Percent Isokinetic of Sampling Rate, % 104.6 106.3 107.3 106.067

Percent Excess Air, % 93.3 94.9 89.4 92.533

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

Round Duct Diameter, inches 264 264 264

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Saturday, January 29, 2011 Page 23 of 31
8/24/2010

Location UNIT 6 - Method 25A

Average

Run Number 1 2 3

Test Date 4/29/2010 4/29/2010 4/29/2010

Run Start Time 8:15:00 AM 11:31:00 AM 3:00:00 PM

Run Finish Time 11:14:00 AM 2:30:00 PM 5:59:00 PM

Carbon Dioxide, % 10.4264 10.4267 10.53 10.461

Oxygen, % 10.0484 9.8808 9.8194 9.916

Fuel Factor 1.04 1.06 1.05

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 0 0 0 0.000

Operating Units PPM PPM PPM

No. Readings/Avg. 180 180 180 180.000

Calibration Set 5 5 5 5.000

Calibration Pre Zero Cylinder ID CC CC CC

Calibration Pre Zero Cylinder Instrument Response 0.26 0.315 0.44 0.338

Calibration Pre Zero Cylinder Bias -0.49 -0.44 -0.32 -0.417

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC205237 CC205237 CC205237

Calibration Pre High Cylinder Instrument Response 49.776 49.662 49.804 49.747

Calibration Pre High Cylinder Bias -0.01 -0.12 0.01 -0.040

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC CC CC

Calibration Post Zero Cylinder Instrument Response 0.315 0.44 0.816 0.524

Calibration Post Zero Cylinder Bias -0.44 -0.32 0.03 -0.243

Calibration Post Zero Cylinder Drift 0.05 0.12 0.35 0.173

Calibration Post High Cylinder ID CC205237 CC205237 CC205237

Calibration Post High Cylinder Instrument Response 0.767 49.804 49.772 33.448

Calibration Post High Cylinder Bias -45.39 0.01 -0.01 -15.130

Calibration Post High Cylinder Drift 45.38 0.13 0.02 15.177

Cavg 0.767 0.575 1.187 0.843

Cavg Units ppmvd ppmvd ppmvd

Cgas 0.9491 0.1979 0.5623 0.570

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

Saturday, January 29, 2011 Page 24 of 31
8/24/2010

Location UNIT 6 - Method 29

Average

Run Number 1 2 3

Test Date 4/28/2010 4/28/2010 4/29/2010

Run Start Time 12:30:00 PM 5:15:00 PM 8:15:00 AM

Run Finish Time 4:55:00 PM 9:35:00 PM 12:35:00 PM

Net Traversing Points 1 1 1

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.4 0.4 0.4 0.400

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9661 0.9661 0.9661 0.966

Barometric Pressure, inches of Mercury 29.528 29.528 29.728 29.595

Average Orifice Meter Differential, inches H2O 1.52 1.58 1.53 1.543

Dry Gas Meter Volume Sampled, cubic feet 172.092 156.245 162.316 163.551

Average Dry Gas Meter Temperature, °F 56.17 57.17 60.50 57.947

Dry Gas Meter Volume Sampled, dscf 168.476 152.689 158.650 159.938

Total Moisture Liquid collected, g 278.6 259.3 269.7 269.200

Volume of Water Vapor, standard cubic feet 13.11 12.21 12.69 12.670

Moisture Content of Stack Gas, % 7.22 7.40 7.41 7.343

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

Dry Mole Fraction 0.9278 0.926 0.9259 0.927

Carbon Dioxide, % 10.49 10.74 10.4264 10.552

Oxygen, % 10.28 10.07 10.0484 10.133

Carbon Monoxide & Nitrogen, % 79.23 79.19 79.5252 79.315

Fuel Factor 1.01 1.01 1.04

Dry Molecular Weight, lb/lb-Mole 30.09 30.12 30.07 30.093

Wet Molecular weight, lb/lb-Mole 29.22 29.22 29.18 29.207

Flue Gas Static Pressure, inches of H2O -0.02 -0.2 -0.15 -0.123

Absolute Flue Gas Pressure, inches of Mercury 29.53 29.51 29.72 29.587

Average Stack Gas Temperature, °F 302.08 302.00 302.46 302.180

Average Velocity Head, inches of H2O 0.099 0.103 0.101 0.101

Average Stack Gas Velocity, feet/second 21.23 21.67 21.40 21.433

Stack Cross-Sectional Area, square feet 380.133 380.133 380.133 380.133

Dry Volumetric Flow Rate, dry scfm 307,203.7 312,783.1 310,862.8 310,283.200

Actual Wet Volumetric Flue Gas Flow Rate, acfm 484,213.4 494,248.9 488,090.8 488,851.033

Percent Isokinetic of Sampling Rate, % 99.5 88.6 92.6 93.567

Percent Excess Air, % 96.6 92.9 91.8 93.767

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

Round Duct Diameter, inches 264 264 264

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Saturday, January 29, 2011 Page 25 of 31
8/24/2010

Location UNIT 6 - Method 3A CO2

Average

Run Number 1 2 3

Test Date 4/29/2010 4/29/2010 4/29/2010

Run Start Time 8:15:00 AM 11:31:00 AM 3:00:00 PM

Run Finish Time 11:14:00 AM 2:30:00 PM 5:59:00 PM

Carbon Dioxide, % 10.426 10.427 10.53 10.461

Oxygen, % 10.0484 9.8808 9.8194 9.916

Fuel Factor 1.04 1.06 1.05

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 0 0 0 0.000

Operating Units % % %

No. Readings/Avg. 180 180 180 180.000

Calibration Set 1 1 1 1.000

Calibration Pre Zero Cylinder ID CC CC CC

Calibration Pre Zero Cylinder Instrument Response 0.104 0.077 0.114 0.098

Calibration Pre Zero Cylinder Bias 0.31 0.14 0.37 0.273

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC27055-CO2 CC27055-

CO2

CC27055-

CO2

Calibration Pre High Cylinder Instrument Response 16.147 16.099 16.045 16.097

Calibration Pre High Cylinder Bias 0.27 -0.02 -0.36 -0.037

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC CC CC

Calibration Post Zero Cylinder Instrument Response 0.077 0.114 0.128 0.106

Calibration Post Zero Cylinder Bias 0.14 0.37 0.45 0.320

Calibration Post Zero Cylinder Drift 0.17 0.23 0.08 0.160

Calibration Post High Cylinder ID CC27055-CO2 CC27055-

CO2

CC27055-

CO2

Calibration Post High Cylinder Instrument Response 16.099 16.045 16.07 16.071

Calibration Post High Cylinder Bias -0.02 -0.36 -0.21 -0.197

Calibration Post High Cylinder Drift 0.29 0.34 0.15 0.260

Cavg 10.499 10.468 10.57 10.512

Cavg Units %vd %vd %vd

Cgas 10.4264 10.4267 10.53 10.461

Cgas Units %vd %vd %vd

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

Saturday, January 29, 2011 Page 26 of 31
8/24/2010

Location UNIT 6 - Method 3A CO2 3

Average

Run Number 4

Test Date 4/29/2010

Run Start Time 6:10:00 PM

Run Finish Time 8:09:00 PM

Carbon Dioxide, % 10.838 10.838

Oxygen, % 9.8876 9.888

Fuel Factor 1.02

Dry Volumetric Flow Rate, dry scfm 0 0.000

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

Moisture, % 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 0 0.000

Operating Units %

No. Readings/Avg. 180 180.000

Calibration Set 1 1.000

Calibration Pre Zero Cylinder ID CC

Calibration Pre Zero Cylinder Instrument Response 0.128 0.128

Calibration Pre Zero Cylinder Bias 0.45 0.450

Calibration Pre Zero Cylinder Drift 0 0.000

Calibration Pre High Cylinder ID CC27055-CO2

Calibration Pre High Cylinder Instrument Response 16.07 16.070

Calibration Pre High Cylinder Bias -0.21 -0.210

Calibration Pre High Cylinder Drift 0 0.000

Calibration Post Zero Cylinder ID CC

Calibration Post Zero Cylinder Instrument Response 0.078 0.078

Calibration Post Zero Cylinder Bias 0.14 0.140

Calibration Post Zero Cylinder Drift 0.31 0.310

Calibration Post High Cylinder ID CC27055-CO2

Calibration Post High Cylinder Instrument Response 15 15.000

Calibration Post High Cylinder Bias 0 0.000

Calibration Post High Cylinder Drift 0 0.000

Cavg 10.517 10.517

Cavg Units %vd

Cgas 10.8378 10.838

Cgas Units %vd

Fuel Type Oil

Fw 10320 10,320.000

Fc 1420 1,420.000

Cgasw 0 0.000

Cgasw Units

Saturday, January 29, 2011 Page 27 of 31
8/24/2010

Location UNIT 6 - Method 3A O2

Average

Run Number 1 2 3

Test Date 4/29/2010 4/29/2010 4/29/2010

Run Start Time 8:15:00 AM 11:31:00 AM 3:00:00 PM

Run Finish Time 11:14:00 AM 2:30:00 PM 5:59:00 PM

Carbon Dioxide, % 10.426 10.427 10.53 10.461

Oxygen, % 10.0484 9.8808 9.8194 9.916

Fuel Factor 1.04 1.06 1.05

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 0 0 0 0.000

Operating Units % % %

No. Readings/Avg. 180 180 180 180.000

Calibration Set 2 2 2 2.000

Calibration Pre Zero Cylinder ID CC CC CC

Calibration Pre Zero Cylinder Instrument Response 0.085 0.122 0.14 0.116

Calibration Pre Zero Cylinder Bias 0.24 0.73 0.88 0.617

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC27055-O2 CC27055-O2 CC27055-O2

Calibration Pre High Cylinder Instrument Response 11.956 11.976 11.98 11.971

Calibration Pre High Cylinder Bias 0.1 0.33 0.37 0.267

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC CC CC

Calibration Post Zero Cylinder Instrument Response 0.122 0.14 0.122 0.128

Calibration Post Zero Cylinder Bias 0.42 0.88 0.73 0.677

Calibration Post Zero Cylinder Drift 0.18 0.15 0.15 0.160

Calibration Post High Cylinder ID CC27055-O2 CC27055-O2 CC27055-O2

Calibration Post High Cylinder Instrument Response 11.976 11.98 12.007 11.988

Calibration Post High Cylinder Bias 0.19 0.37 0.59 0.383

Calibration Post High Cylinder Drift 43.29 0.04 0.22 14.517

Cavg 10.045 9.894 9.846 9.928

Cavg Units %vd %vd %vd

Cgas 10.0484 9.8808 9.8194 9.916

Cgas Units %vd %vd %vd

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

Saturday, January 29, 2011 Page 28 of 31
8/24/2010

Location UNIT 6 - Method 3A O2 3

Average

Run Number 4

Test Date 4/29/2010

Run Start Time 6:10:00 PM

Run Finish Time 8:09:00 PM

Carbon Dioxide, % 10.838 10.838

Oxygen, % 9.8876 9.888

Fuel Factor 1.02

Dry Volumetric Flow Rate, dry scfm 0 0.000

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

Moisture, % 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 0 0.000

Operating Units %

No. Readings/Avg. 180 180.000

Calibration Set 2 2.000

Calibration Pre Zero Cylinder ID CC

Calibration Pre Zero Cylinder Instrument Response 0.122 0.122

Calibration Pre Zero Cylinder Bias 0.73 0.730

Calibration Pre Zero Cylinder Drift 0 0.000

Calibration Pre High Cylinder ID CC27055-O2

Calibration Pre High Cylinder Instrument Response 12.007 12.007

Calibration Pre High Cylinder Bias 0.59 0.590

Calibration Pre High Cylinder Drift 0 0.000

Calibration Post Zero Cylinder ID CC

Calibration Post Zero Cylinder Instrument Response 0.099 0.099

Calibration Post Zero Cylinder Bias 0.53 0.530

Calibration Post Zero Cylinder Drift 0.2 0.200

Calibration Post High Cylinder ID CC27055-O2

Calibration Post High Cylinder Instrument Response 12.041 12.041

Calibration Post High Cylinder Bias 0.88 0.880

Calibration Post High Cylinder Drift 0.29 0.290

Cavg 9.935 9.935

Cavg Units %vd

Cgas 9.8876 9.888

Cgas Units %vd

Fuel Type Oil

Fw 10320 10,320.000

Fc 1420 1,420.000

Cgasw 0 0.000

Cgasw Units

Saturday, January 29, 2011 Page 29 of 31
8/24/2010

Location UNIT 6 - Method 6C

Average

Run Number 1 2 3

Test Date 4/29/2010 4/29/2010 4/29/2010

Run Start Time 8:15:00 AM 11:31:00 AM 3:00:00 PM

Run Finish Time 11:14:00 AM 2:30:00 PM 5:59:00 PM

Carbon Dioxide, % 10.4264 10.4267 10.53 10.461

Oxygen, % 10.0484 9.8808 9.8194 9.916

Fuel Factor 1.04 1.06 1.05

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 0 0 0 0.000

Operating Units PPM PPM PPM

No. Readings/Avg. 180 180 180 180.000

Calibration Set 4 4 4 4.000

Calibration Pre Zero Cylinder ID CC CC CC

Calibration Pre Zero Cylinder Instrument Response 0.6 1.96 1.24 1.267

Calibration Pre Zero Cylinder Bias 0.32 1.68 0.96 0.987

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC121872 CC121872 CC121872

Calibration Pre High Cylinder Instrument Response 48.84 48.56 48.4 48.600

Calibration Pre High Cylinder Bias -0.88 -1.16 -1.32 -1.120

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC CC CC

Calibration Post Zero Cylinder Instrument Response 0.96 1.24 1.32 1.173

Calibration Post Zero Cylinder Bias 0.68 0.96 1.04 0.893

Calibration Post Zero Cylinder Drift 0.36 0.72 8.000000000

00001E-02

0.387

Calibration Post High Cylinder ID CC121872 CC121872 CC121872

Calibration Post High Cylinder Instrument Response 48.62 48.4 48.28 48.433

Calibration Post High Cylinder Bias -1.1 -1.32 -1.44 -1.287

Calibration Post High Cylinder Drift 0.22 0.16 0.12 0.167

Cavg 69.013 72.149 76.707 72.623

Cavg Units ppmvd ppmvd ppmvd

Cgas 69.2006 73.1825 77.9434 73.442

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

Saturday, January 29, 2011 Page 30 of 31
8/24/2010

Location UNIT 6 - OTM - 27/28

Average

Run Number 1 2 3

Test Date 4/28/2010 4/28/2010 4/29/2010

Run Start Time 7:20:00 AM 12:30:00 PM 5:15:00 PM

Run Finish Time 11:45:00 AM 4:55:00 PM 9:35:00 PM

Net Traversing Points 24 24 24

Net Run Time, minutes 244.5 247.5 239.5

Nozzle Diameter, inches 0.32 0.322 0.322 0.321

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9986 0.9986 0.9986 0.999

Barometric Pressure, inches of Mercury 29.71 29.71 29.71 29.710

Average Orifice Meter Differential, inches H2O 0.45 0.45 0.45 0.450

Dry Gas Meter Volume Sampled, cubic feet 89.732 91.960 88.952 90.215

Average Dry Gas Meter Temperature, °F 55.08 55.83 58.88 56.597

Dry Gas Meter Volume Sampled, dscf 91.311 93.442 89.854 91.536

Total Moisture Liquid collected, g 151.8 140.1 139.9 143.933

Volume of Water Vapor, standard cubic feet 7.15 6.59 6.59 6.777

Moisture Content of Stack Gas, % 7.26 6.59 6.83 6.893

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

Dry Mole Fraction 0.9274 0.9341 0.9317 0.931

Carbon Dioxide, % 12.75 12.75 12.75 12.750

Oxygen, % 7 7 7 7.000

Carbon Monoxide & Nitrogen, % 80.25 80.25 80.25 80.250

Fuel Factor 1.09 1.09 1.09

Dry Molecular Weight, lb/lb-Mole 30.32 30.32 30.32 30.320

Wet Molecular weight, lb/lb-Mole 29.43 29.51 29.48 29.473

Flue Gas Static Pressure, inches of H2O -0.2 -0.8 -0.2 -0.400

Absolute Flue Gas Pressure, inches of Mercury 29.70 29.65 29.70 29.683

Average Stack Gas Temperature, °F 302.25 303.25 303.71 303.070

Average Velocity Head, inches of H2O 0.1032221153

12513

0.105726449

602341

9.919540077

21159E-02

0.103

Average Stack Gas Velocity, feet/second 21.55 21.81 21.12 21.493

Stack Cross-Sectional Area, square feet 380.133 380.133 380.133 380.133

Dry Volumetric Flow Rate, dry scfm 313,424.2 318,541.5 308,004.6 313,323.433

Actual Wet Volumetric Flue Gas Flow Rate, acfm 491,512.0 497,442.0 481,704.5 490,219.500

Percent Isokinetic of Sampling Rate, % 81.1 79.7 81.9 80.900

Percent Excess Air, % 49.3 49.3 49.3 49.300

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

Round Duct Diameter, inches 264 264 264

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Saturday, January 29, 2011 Page 31 of 31