Name: C.D. Holley

Title: Vice President F&H System Operatio

Company: Dominion Generation

Sign Date: 8/19/2010

Name: Michael P. Martin

Title: Senior Project Manager

Company: TRC Companies, Inc.

Sign Date: 8/19/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

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.

Thursday, January 13, 2011 Page 1 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

Facility Information:

Southampton Power Station

30134 General Thomas Hwy.

Franklin VA 23851

Contact: David Nuckols

Phone: 804-796-6021

Fax: 804-796-6004

Email: david.nuckols@dom.com

Testing Company:

TRC Companies, Inc.

650 Suffolk Street

Lowell MA 01854

Contact:Michael P. Martin

Phone: 978-656-3550

Fax: 978-453-4215

Email: mmartin@trcsolutions.com

Air Permit Number:

10774

Permitted Source ID/Name:

1_2

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:

Unit 1 & Unit 2 are each a 400 mmBtu/hr spreader stoker coal boiler. Each have overfire air, dry lime FGD, & a 

baghouse.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 5117500051 FRS #: 110000869695

SCC / Description 10100202 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Pulverized Coal: Dry Bottom (Bituminous Coal) 

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 Exit 96 0 0 0 1284 1056 4 6

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Exit Carbon Monoxide Method 10 3 120 0

Stack Exit Formaldehyde Method 0011 3 120 0

Total organic compounds 

(TOC) as Propane

Method 25A 3 120 0 NMHC emissions 

only. Methane 

emissions reported in 

excel template.

Stack Exit

Stack Exit Hydrogen Fluoride Method 26A 3 180 0

Stack Exit Hydrogen Chloride Method 26A 3 180 0

Thursday, January 13, 2011 Page 2 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

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.

Inorganic (Aqueous) 

Condensible Part.

Stack Exit OTM - 27/28 3 240 0

Stack Exit Filterable PM2.5 OTM - 27/28 3 240 0

Organic Condensible 

Particulate

Stack Exit OTM - 27/28 3 240 0

Stack Exit Total PM2.5 OTM - 27/28 3 240 0

Stack Exit Total Particulate OTM - 27/28 3 240 0

Stack Exit Filterable Particulate OTM - 27/28 3 240 0

Stack Exit Cobalt Method 29 3 240 0

Stack Exit Selenium Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Lead Method 29 3 240 0

Stack Exit Chromium Method 29 3 240 0

Stack Exit Cadmium Method 29 3 240 0

Stack Exit Beryllium Method 29 3 240 0

Stack Exit Arsenic Method 29 3 240 0

Stack Exit Antimony Method 29 3 240 0

Stack Exit Sulfur Dioxide Method 6C 3 180 0

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

Thursday, January 13, 2011 Page 3 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

Sampling / Stack Data Results Summary

Location Stack Exit - Method 0011

Average

Run Number 1 2 3

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

Run Start Time

Run Finish Time

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 115.173 112.663 114.636 114.157

Moisture Content of Stack Gas, % 12.52 12.28 11.84 12.213

Moisture Saturation at Stack Gas Temperature, % 66.48 66.24 63.47 65.397

Carbon Dioxide, % 12.605 12.643 12.635 12.628

Oxygen, % 6.535 6.488 6.496 6.506

Average Stack Gas Temperature, °F 191.96 191.79 189.79 191.180

Dry Volumetric Flow Rate, dry scfm 188,189.8 185,918.3 189,619.3 187,909.133

Actual Wet Volumetric Flue Gas Flow Rate, acfm 266,877.0 262,865.8 265,942.1 265,228.300

Percent Isokinetic of Sampling Rate, % 98.9 97.9 97.7 98.167

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack Exit - Method 10

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Thursday, January 13, 2011 Page 4 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

Location Stack Exit - Method 25A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack Exit - Method 26A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Thursday, January 13, 2011 Page 5 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

Location Stack Exit - Method 29 

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Location Stack Exit - Method 6C

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Thursday, January 13, 2011 Page 6 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

Location Stack Exit - Method 7E

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack Exit - OTM - 27/28

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Thursday, January 13, 2011 Page 7 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

Emissions Summary

Location: Stack Exit - Method 0011

Compound: Formaldehyde

Average

RunNumber 1 2 3

Mass_mg 0.0682 0.0518 0.093 0.071

lb/mmBtuO2 1.86E-05 1.44E-05 2.54E-05 0.000

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 3.67E-02 3.22E-02 3.73E-02 0.035

ppm 3.55E+01 3.12E+01 3.62E+01 34.300

ppm@7%O2 3.44E+01 3.01E+01 3.49E+01 33.133

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 -9.77E-07 1.95E-06 0.00E+00 0.000

ppm -6.00E-04 1.20E-03 0.00E+00 0.000

ppm@7%O2 -5.81E-04 1.16E-03 0.00E+00 0.000

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 0.401 0.434 0.45 0.428

lb/mmBtuO2 7.25E-05 7.80E-05 8.24E-05 0.000

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.387 0.419 0.435 0.414

lb/mmBtuO2 6.99E-05 7.53E-05 7.97E-05 0.000

Location: Stack Exit - Method 29 

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.000808 0.000621 0.00053 0.001

lb/mmBtuO2 1.09E-07 8.54E-08 7.14E-08 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.00248 0.00202 0.00171 0.002

lb/mmBtuO2 3.35E-07 2.78E-07 2.30E-07 0.000

Thursday, January 13, 2011 Page 8 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.000476 0.000366 0.000344 0.000

lb/mmBtuO2 6.43E-08 5.03E-08 4.64E-08 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.000327 0.000152 0.00015 0.000

lb/mmBtuO2 4.42E-08 2.09E-08 2.02E-08 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.01287 0.00587 0.00655 0.008

lb/mmBtuO2 1.74E-06 8.07E-07 8.83E-07 0.000

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.00241 0.00178 0.00178 0.002

lb/mmBtuO2 3.26E-07 2.45E-07 2.40E-07 0.000

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.00615 0.00481 0.004294 0.005

lb/mmBtuO2 8.31E-07 6.61E-07 5.79E-07 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.01392 0.00544 0.01838 0.013

lb/mmBtuO2 1.88E-06 7.48E-07 2.48E-06 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.01553 0.01178 0.01239 0.013

lb/mmBtuO2 2.10E-06 1.62E-06 1.67E-06 0.000

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.00359 0.00347 0.00303 0.003

lb/mmBtuO2 4.85E-07 4.77E-07 4.08E-07 0.000

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

lb/mmBtuO2 2.74E-02 2.60E-02 3.27E-02 0.029

Thursday, January 13, 2011 Page 9 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

Process Run Data

ppm 1.14E+01 1.09E+01 1.39E+01 12.067

ppm@7%O2 1.12E+01 1.06E+01 1.34E+01 11.733

Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

lb/mmBtuO2 3.93E-01 3.93E-01 3.90E-01 0.392

ppm 2.28E+02 2.29E+02 2.31E+02 229.333

ppm@7%O2 2.24E+02 2.24E+02 2.23E+02 223.667

Location: Stack Exit - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 2 3 1

Mass_mg 40.4 34.2 40.5 38.367

lb/mmBtuO2 1.02E-02 8.63E-03 9.12E-03 0.009

Compound: Filterable PM2.5

Average

RunNumber 2 3 1

Mass_mg 5.3 4.9 4.4 4.867

lb/mmBtuO2 1.34E-03 1.24E-03 9.91E-04 0.001

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 2 3 1

Mass_mg 5.87 6.27 15.27 9.137

lb/mmBtuO2 1.49E-03 1.58E-03 3.44E-03 0.002

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 8.63 2.13 0.83 3.863

lb/mmBtuO2 1.94E-03 5.40E-04 2.09E-04 0.001

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 64.4 48.4 41.3 51.367

lb/mmBtuO2 1.45E-02 1.23E-02 1.04E-02 0.012

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 28.3 13.3 12 17.867

lb/mmBtuO2 6.37E-03 3.37E-03 3.03E-03 0.004

Thursday, January 13, 2011 Page 10 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Unit 1 & 2 Combined Total Heat Input 1134.7 Million Btus/hr Collected during 

OTM-27/28 run 1

0

1 Unit 1 & 2 Combined Total Steam Output 552.7 1000 lb steam/hr Collected during 

OTM-27/28 run 1

0

1 Unit 1 Flue Gas Flow Rate 397.2 KPPH Collected during 

OTM-27/28 run 1

0

1 Unit 2 Flue Gas Flow Rate 395.9 KPPH Collected during 

OTM-27/28 run 1

0

1 Unit 1 Pressure Drop Across FGD 12.4 in H2O Collected during 

OTM-27/28 run 1

0

1 Unit 2 Pressure Drop Across FGD 13.7 in H2O Collected during 

OTM-27/28 run 1

0

1 Unit 1 FGD Scrubber Liquor Flow Rate 71 gals/min Collected during 

OTM-27/28 run 1

0

1 Unit 2 FGD Scrubber Liquor Flow Rate 66 gals/min Collected during 

OTM-27/28 run 1

0

1 Flue Gas Sampling Point Temperature 189.29 Deg F Collected during 

OTM-27/28 run 1

0

1 Unit 1 & 2 Combined Total Gross Electric 

Generation

68.6 Mwe Collected during 

OTM-27/28 run 1

0

1 Flue Gas Carbon Dioxide Content 10.4 % Collected during 

OTM-27/28 run 1

0

1 Unit 1 & 2 Combined Total Coal Firing Rate 31.12 tons/hr Collected during 

OTM-27/28 run 1

0

1 Unit 1 & 2 Combined Total Net Electric 

Generation

62.9 MWh Collected during 

OTM-27/28 run 1

0

2 Unit 1 & 2 Combined Total Heat Input 789.9 Million Btus/hr Collected during 

OTM-27/28 run 2

0

2 Unit 1 & 2 Combined Total Steam Output 543.5 1000 lb steam/hr Collected during 

OTM-27/28 run 2

0

2 Unit 1 Flue Gas Flow Rate 369.2 KPPH Collected during 

OTM-27/28 run 2

0

2 Unit 2 Flue Gas Flow Rate 370.9 KPPH Collected during 

OTM-27/28 run 2

0

2 Unit 1 Pressure Drop Across FGD 10.5 in H2O Collected during 

OTM-27/28 run 2

0

2 Unit 2 Pressure Drop Across FGD 12.6 in H2O Collected during 

OTM-27/28 run 2

0

2 Unit 1 FGD Scrubber Liquor Flow Rate 66 gals/min Collected during 

OTM-27/28 run 2

0

2 Unit 2 FGD Scrubber Liquor Flow Rate 63 gals/min Collected during 

OTM-27/28 run 2

0

Thursday, January 13, 2011 Page 11 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

2 Flue Gas Sampling Point Temperature 187.15 Deg F Collected during 

OTM-27/28 run 2

0

2 Unit 1 & 2 Combined Total Gross Electric 

Generation

68.5 Mwe Collected during 

OTM-27/28 run 2

0

2 Flue Gas Carbon Dioxide Content 11.2 % Collected during 

OTM-27/28 run 2

0

2 Unit 1 & 2 Combined Total Coal Firing Rate 31.48 tons/hr Collected during 

OTM-27/28 run 2

0

2 Unit 1 & 2 Combined Total Net Electric 

Generation

62.7 MWh Collected during 

OTM-27/28 run 2

0

3 Unit 1 & 2 Combined Total Heat Input 791.8 Million Btus/hr Collected during 

OTM-27/28 run 3

0

3 Unit 1 & 2 Combined Total Steam Output 545.2 1000 lb steam/hr Collected during 

OTM-27/28 run 3

0

3 Unit 1 Flue Gas Flow Rate 372.8 KPPH Collected during 

OTM-27/28 run 3

0

3 Unit 2 Flue Gas Flow Rate 369.7 KPPH Collected during 

OTM-27/28 run 3

0

3 Unit 1 Pressure Drop Across FGD 10.9 in H2O Collected during 

OTM-27/28 run 3

0

3 Unit 2 Pressure Drop Across FGD 12.5 in H2O Collected during 

OTM-27/28 run 3

0

3 Unit 1 FGD Scrubber Liquor Flow Rate 64 gals/min Collected during 

OTM-27/28 run 3

0

3 Unit 2 FGD Scrubber Liquor Flow Rate 70 gals/min Collected during 

OTM-27/28 run 3

0

3 Flue Gas Sampling Point Temperature 185.4 Deg F Collected during 

OTM-27/28 run 3

0

3 Unit 1 & 2 Combined Total Gross Electric 

Generation

68.6 Mwe Collected during 

OTM-27/28 run 3

0

3 Flue Gas Carbon Dioxide Content 11.3 % Collected during 

OTM-27/28 run 3

0

3 Unit 1 & 2 Combined Total Coal Firing Rate 31.48 tons/hr Collected during 

OTM-27/28 run 3

0

3 Unit 1 & 2 Combined Total Net Electric 

Generation

63.2 MWh Collected during 

OTM-27/28 run 3

0

4 Unit 1 & 2 Combined Total Heat Input 1060.4 Million Btus/hr Collected during 

M29 run 1

0

4 Unit 1 & 2 Combined Total Steam Output 553 1000 lb steam/hr Collected during 

M29 run 1

0

4 Unit 1 Flue Gas Flow Rate 402.8 KPPH Collected during 

M29 run 1

0

4 Unit 2 Flue Gas Flow Rate 402.8 KPPH Collected during 

M29 run 1

0

4 Unit 1 Pressure Drop Across FGD 12.9 in H2O Collected during 

M29 run 1

0

Thursday, January 13, 2011 Page 12 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

4 Unit 2 Pressure Drop Across FGD 13.9 in H2O Collected during 

M29 run 1

0

4 Unit 1 FGD Scrubber Liquor Flow Rate 72 gals/min Collected during 

M29 run 1

0

4 Unit 2 FGD Scrubber Liquor Flow Rate 67 gals/min Collected during 

M29 run 1

0

4 Flue Gas Sampling Point Temperature 189.81 Deg F Collected during 

M29 run 1

0

4 Unit 1 & 2 Combined Total Gross Electric 

Generation

68.7 Mwe Collected during 

M29 run 1

0

4 Flue Gas Carbon Dioxide Content 10.4 % Collected during 

M29 run 1

0

4 Unit 1 & 2 Combined Total Coal Firing Rate 31.12 tons/hr Collected during 

M29 run 1

0

4 Unit 1 & 2 Combined Total Net Electric 

Generation

63.1 MWh Collected during 

M29 run 1

0

5 Unit 1 & 2 Combined Total Heat Input 788.2 Million Btus/hr Collected during 

M29 run 2

0

5 Unit 1 & 2 Combined Total Steam Output 543.3 1000 lb steam/hr Collected during 

M29 run 2

0

5 Unit 1 Flue Gas Flow Rate 372.6 KPPH Collected during 

M29 run 2

0

5 Unit 2 Flue Gas Flow Rate 374.1 KPPH Collected during 

M29 run 2

0

5 Unit 1 Pressure Drop Across FGD 10.8 in H2O Collected during 

M29 run 2

0

5 Unit 2 Pressure Drop Across FGD 12.9 in H2O Collected during 

M29 run 2

0

5 Unit 1 FGD Scrubber Liquor Flow Rate 67 gals/min Collected during 

M29 run 2

0

5 Unit 2 FGD Scrubber Liquor Flow Rate 63 gals/min Collected during 

M29 run 2

0

5 Flue Gas Sampling Point Temperature 187.01 Deg F Collected during 

M29 run 2

0

5 Unit 1 & 2 Combined Total Gross Electric 

Generation

68.4 Mwe Collected during 

M29 run 2

0

5 Flue Gas Carbon Dioxide Content 11.2 % Collected during 

M29 run 2

0

5 Unit 1 & 2 Combined Total Coal Firing Rate 31.48 tons/hr Collected during 

M29 run 2

0

5 Unit 1 & 2 Combined Total Net Electric 

Generation

62.6 MWh Collected during 

M29 run 2

0

6 Unit 1 & 2 Combined Total Heat Input 792.9 Million Btus/hr Collected during 

M29 run 3

0

6 Unit 1 & 2 Combined Total Steam Output 546.3 1000 lb steam/hr Collected during 

M29 run 3

0

Thursday, January 13, 2011 Page 13 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

6 Unit 1 Flue Gas Flow Rate 372.8 KPPH Collected during 

M29 run 3

0

6 Unit 2 Flue Gas Flow Rate 369.6 KPPH Collected during 

M29 run 3

0

6 Unit 1 Pressure Drop Across FGD 11 in H2O Collected during 

M29 run 3

0

6 Unit 2 Pressure Drop Across FGD 12.6 in H2O Collected during 

M29 run 3

0

6 Unit 1 FGD Scrubber Liquor Flow Rate 64 gals/min Collected during 

M29 run 3

0

6 Unit 2 FGD Scrubber Liquor Flow Rate 69 gals/min Collected during 

M29 run 3

0

6 Flue Gas Sampling Point Temperature 185.55 Deg F Collected during 

M29 run 3

0

6 Unit 1 & 2 Combined Total Gross Electric 

Generation

68.4 Mwe Collected during 

M29 run 3

0

6 Flue Gas Carbon Dioxide Content 11.3 % Collected during 

M29 run 3

0

6 Unit 1 & 2 Combined Total Coal Firing Rate 31.48 tons/hr Collected during 

M29 run 3

0

6 Unit 1 & 2 Combined Total Net Electric 

Generation

63.3 MWh Collected during 

M29 run 3

0

7 Unit 1 & 2 Combined Total Heat Input 802.5 Million Btus/hr Collected during 

run 1 of M0011 

and run 1 of 

Method 10 and 

25A

0

7 Unit 1 & 2 Combined Total Steam Output 545.5 1000 lb steam/hr Collected during 

run 1 of M0011 

and run 1 of 

Method 10 and 

25A

0

7 Unit 1 Flue Gas Flow Rate 379 KPPH Collected during 

run 1 of M0011 

and run 1 of 

Method 10 and 

25A

0

7 Unit 2 Flue Gas Flow Rate 389.1 KPPH Collected during 

run 1 of M0011 

and run 1 of 

Method 10 and 

25A

0

7 Unit 1 Pressure Drop Across FGD 12.4 in H2O Collected during 

run 1 of M0011 

and run 1 of 

Method 10 and 

25A

0

Thursday, January 13, 2011 Page 14 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

7 Unit 2 Pressure Drop Across FGD 13 in H2O Collected during 

run 1 of M0011 

and run 1 of 

Method 10 and 

25A

0

7 Unit 1 FGD Scrubber Liquor Flow Rate 63 gals/min Collected during 

run 1 of M0011 

and run 1 of 

Method 10 and 

25A

0

7 Unit 2 FGD Scrubber Liquor Flow Rate 61 gals/min Collected during 

run 1 of M0011 

and run 1 of 

Method 10 and 

25A

0

7 Flue Gas Sampling Point Temperature 191.56 Deg F Collected during 

run 1 of M0011 

and run 1 of 

Method 10 and 

25A

0

7 Unit 1 & 2 Combined Total Gross Electric 

Generation

68.6 Mwe Collected during 

run 1 of M0011 

and run 1 of 

Method 10 and 

25A

0

7 Flue Gas Carbon Dioxide Content 11 % Collected during 

run 1 of M0011 

and run 1 of 

Method 10 and 

25A

0

7 Unit 1 & 2 Combined Total Coal Firing Rate 27.76 tons/hr Collected during 

run 1 of M0011 

and run 1 of 

Method 10 and 

25A

0

7 Unit 1 & 2 Combined Total Net Electric 

Generation

62.9 MWh Collected during 

run 1 of M0011 

and run 1 of 

Method 10 and 

25A

0

8 Unit 1 & 2 Combined Total Heat Input 800.1 Million Btus/hr Collected during 

run 2 of M0011 

and run 2 of 

Method 10 and 

25A

0

8 Unit 1 & 2 Combined Total Steam Output 545.5 1000 lb steam/hr Collected during 

run 2 of M0011 

and run 2 of 

Method 10 and 

25A

0

Thursday, January 13, 2011 Page 15 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

8 Unit 1 Flue Gas Flow Rate 379.9 KPPH Collected during 

run 2 of M0011 

and run 2 of 

Method 10 and 

25A

0

8 Unit 2 Flue Gas Flow Rate 383.6 KPPH Collected during 

run 2 of M0011 

and run 2 of 

Method 10 and 

25A

0

8 Unit 1 Pressure Drop Across FGD 11.6 in H2O Collected during 

run 2 of M0011 

and run 2 of 

Method 10 and 

25A

0

8 Unit 2 Pressure Drop Across FGD 13.6 in H2O Collected during 

run 2 of M0011 

and run 2 of 

Method 10 and 

25A

0

8 Unit 1 FGD Scrubber Liquor Flow Rate 63 gals/min Collected during 

run 2 of M0011 

and run 2 of 

Method 10 and 

25A

0

8 Unit 2 FGD Scrubber Liquor Flow Rate 61 gals/min Collected during 

run 2 of M0011 

and run 2 of 

Method 10 and 

25A

0

8 Flue Gas Sampling Point Temperature 191.74 Deg F Collected during 

run 2 of M0011 

and run 2 of 

Method 10 and 

25A

0

8 Unit 1 & 2 Combined Total Gross Electric 

Generation

68.9 Mwe Collected during 

run 2 of M0011 

and run 2 of 

Method 10 and 

25A

0

8 Flue Gas Carbon Dioxide Content 11 % Collected during 

run 2 of M0011 

and run 2 of 

Method 10 and 

25A

0

8 Unit 1 & 2 Combined Total Coal Firing Rate 27.76 tons/hr Collected during 

run 2 of M0011 

and run 2 of 

Method 10 and 

25A

0

Thursday, January 13, 2011 Page 16 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

8 Unit 1 & 2 Combined Total Net Electric 

Generation

63 MWh Collected during 

run 2 of M0011 

and run 2 of 

Method 10 and 

25A

0

9 Unit 1 & 2 Combined Total Heat Input 796.6 Million Btus/hr Collected during 

run 3 of M0011 

and run 3 of 

Method 10 and 

25A

0

9 Unit 1 & 2 Combined Total Steam Output 546 1000 lb steam/hr Collected during 

run 3 of M0011 

and run 3 of 

Method 10 and 

25A

0

9 Unit 1 Flue Gas Flow Rate 380.8 KPPH Collected during 

run 3 of M0011 

and run 3 of 

Method 10 and 

25A

0

9 Unit 2 Flue Gas Flow Rate 378.1 KPPH Collected during 

run 3 of M0011 

and run 3 of 

Method 10 and 

25A

0

9 Unit 1 Pressure Drop Across FGD 11 in H2O Collected during 

run 3 of M0011 

and run 3 of 

Method 10 and 

25A

0

9 Unit 2 Pressure Drop Across FGD 13.5 in H2O Collected during 

run 3 of M0011 

and run 3 of 

Method 10 and 

25A

0

9 Unit 1 FGD Scrubber Liquor Flow Rate 65 gals/min Collected during 

run 3 of M0011 

and run 3 of 

Method 10 and 

25A

0

9 Unit 2 FGD Scrubber Liquor Flow Rate 62 gals/min Collected during 

run 3 of M0011 

and run 3 of 

Method 10 and 

25A

0

9 Flue Gas Sampling Point Temperature 190.23 Deg F Collected during 

run 3 of M0011 

and run 3 of 

Method 10 and 

25A

0

Thursday, January 13, 2011 Page 17 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

9 Unit 1 & 2 Combined Total Gross Electric 

Generation

68.8 Mwe Collected during 

run 3 of M0011 

and run 3 of 

Method 10 and 

25A

0

9 Flue Gas Carbon Dioxide Content 10.9 % Collected during 

run 3 of M0011 

and run 3 of 

Method 10 and 

25A

0

9 Unit 1 & 2 Combined Total Coal Firing Rate 27.76 tons/hr Collected during 

run 3 of M0011 

and run 3 of 

Method 10 and 

25A

0

9 Unit 1 & 2 Combined Total Net Electric 

Generation

63 MWh Collected during 

run 3 of M0011 

and run 3 of 

Method 10 and 

25A

0

10 Unit 1 & 2 Combined Total Heat Input 827.5 Million Btus/hr Collected during 

M26A run 1

0

10 Unit 1 & 2 Combined Total Steam Output 545.3 1000 lb steam/hr Collected during 

M26A run 1

0

10 Unit 1 Flue Gas Flow Rate 390 KPPH Collected during 

M26A run 1

0

10 Unit 2 Flue Gas Flow Rate 382.2 KPPH Collected during 

M26A run 1

0

10 Unit 1 Pressure Drop Across FGD 13.3 in H2O Collected during 

M26A run 1

0

10 Unit 2 Pressure Drop Across FGD 13.6 in H2O Collected during 

M26A run 1

0

10 Unit 1 FGD Scrubber Liquor Flow Rate 64 gals/min Collected during 

M26A run 1

0

10 Unit 2 FGD Scrubber Liquor Flow Rate 59 gals/min Collected during 

M26A run 1

0

10 Flue Gas Sampling Point Temperature 192.91 Deg F Collected during 

M26A run 1

0

10 Unit 1 & 2 Combined Total Gross Electric 

Generation

68.8 Mwe Collected during 

M26A run 1

0

10 Flue Gas Carbon Dioxide Content 11 % Collected during 

M26A run 1

0

10 Unit 1 & 2 Combined Total Coal Firing Rate 24.72 tons/hr Collected during 

M26A run 1

0

10 Unit 1 & 2 Combined Total Net Electric 

Generation

63.2 MWh Collected during 

M26A run 1

0

11 Unit 1 & 2 Combined Total Heat Input 814 Million Btus/hr Collected during 

M26A run 2

0

Thursday, January 13, 2011 Page 18 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

11 Unit 1 & 2 Combined Total Steam Output 550 1000 lb steam/hr Collected during 

M26A run 2

0

11 Unit 1 Flue Gas Flow Rate 390.5 KPPH Collected during 

M26A run 2

0

11 Unit 2 Flue Gas Flow Rate 379.8 KPPH Collected during 

M26A run 2

0

11 Unit 1 Pressure Drop Across FGD 12.5 in H2O Collected during 

M26A run 2

0

11 Unit 2 Pressure Drop Across FGD 13.3 in H2O Collected during 

M26A run 2

0

11 Unit 1 FGD Scrubber Liquor Flow Rate 66 gals/min Collected during 

M26A run 2

0

11 Unit 2 FGD Scrubber Liquor Flow Rate 63 gals/min Collected during 

M26A run 2

0

11 Flue Gas Sampling Point Temperature 192.83 Deg F Collected during 

M26A run 2

0

11 Unit 1 & 2 Combined Total Gross Electric 

Generation

68.7 Mwe Collected during 

M26A run 2

0

11 Flue Gas Carbon Dioxide Content 11.1 % Collected during 

M26A run 2

0

11 Unit 1 & 2 Combined Total Coal Firing Rate 24.72 tons/hr Collected during 

M26A run 2

0

11 Unit 1 & 2 Combined Total Net Electric 

Generation

63 MWh Collected during 

M26A run 2

0

12 Unit 1 & 2 Combined Total Heat Input 811 Million Btus/hr Collected during 

M26A run 3

0

12 Unit 1 & 2 Combined Total Steam Output 551.7 1000 lb steam/hr Collected during 

M26A run 3

0

12 Unit 1 Flue Gas Flow Rate 386.5 KPPH Collected during 

M26A run 3

0

12 Unit 2 Flue Gas Flow Rate 377.2 KPPH Collected during 

M26A run 3

0

12 Unit 1 Pressure Drop Across FGD 12.5 in H2O Collected during 

M26A run 3

0

12 Unit 2 Pressure Drop Across FGD 13.2 in H2O Collected during 

M26A run 3

0

12 Unit 1 FGD Scrubber Liquor Flow Rate 66 gals/min Collected during 

M26A run 3

0

12 Unit 2 FGD Scrubber Liquor Flow Rate 62 gals/min Collected during 

M26A run 3

0

12 Flue Gas Sampling Point Temperature 192.81 Deg F Collected during 

M26A run 3

0

12 Unit 1 & 2 Combined Total Gross Electric 

Generation

68.7 Mwe Collected during 

M26A run 3

0

12 Flue Gas Carbon Dioxide Content 11.1 % Collected during 

M26A run 3

0

Thursday, January 13, 2011 Page 19 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

12 Unit 1 & 2 Combined Total Coal Firing Rate 24.72 tons/hr Collected during 

M26A run 3

0

12 Unit 1 & 2 Combined Total Net Electric 

Generation

63.2 MWh Collected during 

M26A run 3

0

13 Unit 1 & 2 Combined Total Heat Input 823.3 Million Btus/hr Collected during 

run 1 of Method 

6C and 7E

0

13 Unit 1 & 2 Combined Total Steam Output 546 1000 lb steam/hr Collected during 

run 1 of Method 

6C and 7E

0

13 Unit 1 Flue Gas Flow Rate 390.5 KPPH Collected during 

run 1 of Method 

6C and 7E

0

13 Unit 2 Flue Gas Flow Rate 382.2 KPPH Collected during 

run 1 of Method 

6C and 7E

0

13 Unit 1 Pressure Drop Across FGD 13.1 in H2O Collected during 

run 1 of Method 

6C and 7E

0

13 Unit 2 Pressure Drop Across FGD 13.6 in H2O Collected during 

run 1 of Method 

6C and 7E

0

13 Unit 1 FGD Scrubber Liquor Flow Rate 65 gals/min Collected during 

run 1 of Method 

6C and 7E

0

13 Unit 2 FGD Scrubber Liquor Flow Rate 60 gals/min Collected during 

run 1 of Method 

6C and 7E

0

13 Flue Gas Sampling Point Temperature 192.69 Deg F Collected during 

run 1 of Method 

6C and 7E

0

13 Unit 1 & 2 Combined Total Gross Electric 

Generation

68.8 Mwe Collected during 

run 1 of Method 

6C and 7E

0

13 Flue Gas Carbon Dioxide Content 11 % Collected during 

run 1 of Method 

6C and 7E

0

13 Unit 1 & 2 Combined Total Coal Firing Rate 24.72 tons/hr Collected during 

run 1 of Method 

6C and 7E

0

13 Unit 1 & 2 Combined Total Net Electric 

Generation

63.1 MWh Collected during 

run 1 of Method 

6C and 7E

0

14 Unit 1 & 2 Combined Total Heat Input 816.7 Million Btus/hr Collected during 

run 2 of Method 

6C and 7E

0

14 Unit 1 & 2 Combined Total Steam Output 551.3 1000 lb steam/hr Collected during 

run 2 of Method 

6C and 7E

0

Thursday, January 13, 2011 Page 20 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

14 Unit 1 Flue Gas Flow Rate 388.8 KPPH Collected during 

run 2 of Method 

6C and 7E

0

14 Unit 2 Flue Gas Flow Rate 377.8 KPPH Collected during 

run 2 of Method 

6C and 7E

0

14 Unit 1 Pressure Drop Across FGD 12.5 in H2O Collected during 

run 2 of Method 

6C and 7E

0

14 Unit 2 Pressure Drop Across FGD 13.6 in H2O Collected during 

run 2 of Method 

6C and 7E

0

14 Unit 1 FGD Scrubber Liquor Flow Rate 66 gals/min Collected during 

run 2 of Method 

6C and 7E

0

14 Unit 2 FGD Scrubber Liquor Flow Rate 62 gals/min Collected during 

run 2 of Method 

6C and 7E

0

14 Flue Gas Sampling Point Temperature 192.99 Deg F Collected during 

run 2 of Method 

6C and 7E

0

14 Unit 1 & 2 Combined Total Gross Electric 

Generation

68.6 Mwe Collected during 

run 2 of Method 

6C and 7E

0

14 Flue Gas Carbon Dioxide Content 11.1 % Collected during 

run 2 of Method 

6C and 7E

0

14 Unit 1 & 2 Combined Total Coal Firing Rate 24.72 tons/hr Collected during 

run 2 of Method 

6C and 7E

0

14 Unit 1 & 2 Combined Total Net Electric 

Generation

63.3 MWh Collected during 

run 2 of Method 

6C and 7E

0

15 Unit 1 & 2 Combined Total Heat Input 808.5 Million Btus/hr Collected during 

run 3 of Method 

6C and 7E

0

15 Unit 1 & 2 Combined Total Steam Output 551 1000 lb steam/hr Collected during 

run 3 of Method 

6C and 7E

0

15 Unit 1 Flue Gas Flow Rate 385.3 KPPH Collected during 

run 3 of Method 

6C and 7E

0

15 Unit 2 Flue Gas Flow Rate 377.5 KPPH Collected during 

run 3 of Method 

6C and 7E

0

15 Unit 1 Pressure Drop Across FGD 12.3 in H2O Collected during 

run 3 of Method 

6C and 7E

0

Thursday, January 13, 2011 Page 21 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

APCD Run Data

Process Lab Run Data

15 Unit 2 Pressure Drop Across FGD 13.6 in H2O Collected during 

run 3 of Method 

6C and 7E

0

15 Unit 1 FGD Scrubber Liquor Flow Rate 65 gals/min Collected during 

run 3 of Method 

6C and 7E

0

15 Unit 2 FGD Scrubber Liquor Flow Rate 63 gals/min Collected during 

run 3 of Method 

6C and 7E

0

15 Flue Gas Sampling Point Temperature 193 Deg F Collected during 

run 3 of Method 

6C and 7E

0

15 Unit 1 & 2 Combined Total Gross Electric 

Generation

68.8 Mwe Collected during 

run 3 of Method 

6C and 7E

0

15 Flue Gas Carbon Dioxide Content 11.1 % Collected during 

run 3 of Method 

6C and 7E

0

15 Unit 1 & 2 Combined Total Coal Firing Rate 24.72 tons/hr Collected during 

run 3 of Method 

6C and 7E

0

15 Unit 1 & 2 Combined Total Net Electric 

Generation

63.1 MWh Collected during 

run 3 of Method 

6C and 7E

0

Run Name Value UOM Comments

Target

Value

1 OVERFIRE AIR 0 0

1 DRY LIMESTONE INJECTION 0 0

1 BAGHOUSE 0 0

Thursday, January 13, 2011 Page 22 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

Sampling / Stack Data Results Detail

Location Stack Exit - Method 0011

Average

Run Number 1 2 3

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

Run Start Time

Run Finish Time

Net Traversing Points 24 24 24

Net Run Time, minutes 120 120 120

Nozzle Diameter, inches 0.218 0.218 0.218 0.218

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9873 0.9873 0.9873 0.987

Barometric Pressure, inches of Mercury 29.85 29.85 29.85 29.850

Average Orifice Meter Differential, inches H2O 3.10 3.02 3.11 3.077

Dry Gas Meter Volume Sampled, cubic feet 117.488 115.681 118.602 117.257

Average Dry Gas Meter Temperature, °F 74.58 77.98 82.19 78.250

Dry Gas Meter Volume Sampled, dscf 115.173 112.663 114.636 114.157

Total Moisture Liquid collected, g 350.2 335.1 327 337.433

Volume of Water Vapor, standard cubic feet 16.48 15.77 15.39 15.880

Moisture Content of Stack Gas, % 12.52 12.28 11.84 12.213

Moisture Saturation at Stack Gas Temperature, % 66.48 66.24 63.47 65.397

Dry Mole Fraction 0.8748 0.8772 0.8816 0.878

Carbon Dioxide, % 12.605 12.643 12.635 12.628

Oxygen, % 6.535 6.488 6.496 6.506

Carbon Monoxide & Nitrogen, % 80.86 80.869 80.869 80.866

Fuel Factor 1.14 1.14 1.14

Dry Molecular Weight, lb/lb-Mole 30.28 30.28 30.28 30.280

Wet Molecular weight, lb/lb-Mole 28.74 28.77 28.83 28.780

Flue Gas Static Pressure, inches of H2O -0.92 -0.92 -0.92 -0.920

Absolute Flue Gas Pressure, inches of Mercury 29.78 29.78 29.78 29.780

Average Stack Gas Temperature, °F 191.96 191.79 189.79 191.180

Average Velocity Head, inches of H2O 1.9933121890

6302

1.936510857

97195

1.992462675

75771

1.974

Average Stack Gas Velocity, feet/second 88.49 87.16 88.18 87.943

Stack Cross-Sectional Area, square feet 50.265 50.265 50.265 50.265

Dry Volumetric Flow Rate, dry scfm 188,189.8 185,918.3 189,619.3 187,909.133

Actual Wet Volumetric Flue Gas Flow Rate, acfm 266,877.0 262,865.8 265,942.1 265,228.300

Percent Isokinetic of Sampling Rate, % 98.9 97.9 97.7 98.167

Percent Excess Air, % 44.1 43.7 43.7 43.833

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Round Duct Diameter, inches 96 96 96

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Thursday, January 13, 2011 Page 23 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

Location Stack Exit - Method 10

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Thursday, January 13, 2011 Page 24 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

Location Stack Exit - Method 25A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Thursday, January 13, 2011 Page 25 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

Location Stack Exit - Method 26A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Thursday, January 13, 2011 Page 26 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

Location Stack Exit - Method 29 

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Thursday, January 13, 2011 Page 27 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

Location Stack Exit - Method 6C

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Thursday, January 13, 2011 Page 28 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

Location Stack Exit - Method 7E

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Thursday, January 13, 2011 Page 29 of 30
Utility Boiler MACT ICR - Southampton Power Station Units 1 & 2

8/19/2010

Location Stack Exit - OTM - 27/28

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Thursday, January 13, 2011 Page 30 of 30