Name: Katheryn Curtis

Title: Vice President F&H Merchant Operati

Company: Dominion Generation

Sign Date: 10/1/2010

Name: Michael P. Martin

Title: Senior Project Manager

Company: TRC Companies, Inc.

Sign Date: 9/27/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Utility Boiler MACT ICR - Salem Harbor Unit 1

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 26
Utility Boiler MACT ICR - Salem Harbor Unit 1

10/1/2010

Facility Information:

Salem Harbor

24 Fort Avenue

Salem MA 01970

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:

1626

Permitted Source ID/Name:

1

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:

954 mmBtu/hr dry bottom, wall fired, pulverized coal boiler w/ LNB, SNCR, & ESP.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 2511900194 FRS #: 110000310459

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 108 0 0 0 2520 3000 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 26
Utility Boiler MACT ICR - Salem Harbor Unit 1

10/1/2010

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 26
Utility Boiler MACT ICR - Salem Harbor Unit 1

10/1/2010

Sampling / Stack Data Results Summary

Location Stack Exit - Method 0011

Average

Run Number 1 2 3

Test Date 5/7/2010 5/7/2010 5/7/2010

Run Start Time

Run Finish Time

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 101.713 100.353 97.510 99.859

Moisture Content of Stack Gas, % 8.05 8.24 7.98 8.090

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

Carbon Dioxide, % 10.67 11.101 11.414 11.062

Oxygen, % 9.139 8.645 8.295 8.693

Average Stack Gas Temperature, °F 282.88 286.50 289.50 286.293

Dry Volumetric Flow Rate, dry scfm 152,364.3 150,352.4 147,471.3 150,062.667

Actual Wet Volumetric Flue Gas Flow Rate, acfm 234,708.6 233,219.9 229,021.2 232,316.567

Percent Isokinetic of Sampling Rate, % 96.7 96.7 95.8 96.400

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 1 2 3

Test Date 5/7/2010 5/7/2010 5/7/2010

Run Start Time 10:55:00 AM 4:24:00 PM 6:48:00 PM

Run Finish Time 12:55:00 PM 6:24:00 PM 8:48:00 PM

Carbon Dioxide, % 10.67 11.101 11.414 11.062

Oxygen, % 9.139 8.645 8.295 8.693

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Thursday, January 13, 2011 Page 4 of 26
Utility Boiler MACT ICR - Salem Harbor Unit 1

10/1/2010

Location Stack Exit - Method 25A

Average

Run Number 1 2 3

Test Date 5/7/2010 5/7/2010 5/7/2010

Run Start Time 10:55:00 AM 4:24:00 PM 6:48:00 PM

Run Finish Time 12:55:00 PM 6:24:00 PM 8:48:00 PM

Carbon Dioxide, %

Oxygen, % 9.139 8.645 8.295 8.693

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 8.17 8.29 8.16 8.207

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack Exit - Method 26A

Average

Run Number 2 3 4

Test Date 5/6/2010 5/6/2010 5/6/2010

Run Start Time

Run Finish Time

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 139.293 137.320 134.890 137.168

Moisture Content of Stack Gas, % 11.75 12.71 11.39 11.950

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

Carbon Dioxide, % 13.1 13.2 12.5 12.933

Oxygen, % 6.3 6.2 7.1 6.533

Average Stack Gas Temperature, °F 290.33 294.94 295.08 293.450

Dry Volumetric Flow Rate, dry scfm 133,661.4 129,782.7 128,346.4 130,596.833

Actual Wet Volumetric Flue Gas Flow Rate, acfm 218,371.7 217,379.3 211,882.8 215,877.933

Percent Isokinetic of Sampling Rate, % 100.7 102.2 101.5 101.467

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

Thursday, January 13, 2011 Page 5 of 26
Utility Boiler MACT ICR - Salem Harbor Unit 1

10/1/2010

Location Stack Exit - Method 29

Average

Run Number 1 2 3

Test Date 5/4/2010 5/4/2010 5/5/2010

Run Start Time

Run Finish Time

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 206.602 209.232 193.995 203.276

Moisture Content of Stack Gas, % 8.41 8.86 9.23 8.833

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

Carbon Dioxide, % 11.746 11.61 12.857 12.071

Oxygen, % 7.899 8.052 6.685 7.545

Average Stack Gas Temperature, °F 296.56 300.48 289.15 295.397

Dry Volumetric Flow Rate, dry scfm 152,034.0 154,876.7 142,972.4 149,961.033

Actual Wet Volumetric Flue Gas Flow Rate, acfm 239,289.0 246,236.0 223,333.8 236,286.267

Percent Isokinetic of Sampling Rate, % 99.2 98.6 99.1 98.967

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 6C

Average

Run Number 1 2 3

Test Date 5/6/2010 5/6/2010 5/6/2010

Run Start Time 7:01:00 AM 10:18:00 

AM

2:25:00 PM

Run Finish Time 10:01:00 AM 1:18:00 PM 5:25:00 PM

Carbon Dioxide, % 13.13 13.229 12.47 12.943

Oxygen, % 6.342 6.208 7.11 6.553

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Thursday, January 13, 2011 Page 6 of 26
Utility Boiler MACT ICR - Salem Harbor Unit 1

10/1/2010

Location Stack Exit - Method 7E

Average

Run Number 1 2 3

Test Date 5/6/2010 5/6/2010 5/6/2010

Run Start Time 7:01:00 AM 10:18:00 

AM

2:25:00 PM

Run Finish Time 10:01:00 AM 1:18:00 PM 5:25:00 PM

Carbon Dioxide, % 13.13 13.229 12.47 12.943

Oxygen, % 6.342 6.208 7.11 6.553

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack Exit - OTM - 27/28

Average

Run Number 1 2 3

Test Date 5/4/2010 5/4/2010 5/5/2010

Run Start Time

Run Finish Time

Net Run Time, minutes 345.25 330.75 308.75

Dry Gas Meter Volume Sampled, dscf 126.638 122.880 119.158 122.892

Moisture Content of Stack Gas, % 8.91 8.82 8.99 8.907

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

Carbon Dioxide, % 11.75 11.61 12.86 12.073

Oxygen, % 7.899 8.052 6.685 7.545

Average Stack Gas Temperature, °F 295.08 299.92 288.33 294.443

Dry Volumetric Flow Rate, dry scfm 152,425.9 151,860.9 144,229.9 149,505.567

Actual Wet Volumetric Flue Gas Flow Rate, acfm 242,380.8 245,701.6 225,967.6 238,016.667

Percent Isokinetic of Sampling Rate, % 91.7 93.2 101.9 95.600

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

Thursday, January 13, 2011 Page 7 of 26
Utility Boiler MACT ICR - Salem Harbor Unit 1

10/1/2010

Emissions Summary

Location: Stack Exit - Method 0011

Compound: Formaldehyde

Average

RunNumber 1 2 3

Mass_mg 0.0388 0.0417 0.0328 0.038

lb/mmBtuO2 1.46E-05 1.53E-05 1.20E-05 0.000

ppm 1.08E-02 1.18E-02 9.51E-03 0.011

ppm@7%O2 1.28E-02 1.34E-02 1.05E-02 0.012

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 1.69E-02 1.60E-02 1.46E-02 0.016

ppm 1.33E+01 1.32E+01 1.24E+01 12.967

ppm@7%O2 1.57E+01 1.50E+01 1.37E+01 14.800

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 3.45E-04 1.05E-03 6.47E-04 0.001

ppm 1.73E-01 5.52E-01 3.49E-01 0.358

ppm@7%O2 2.04E-01 6.26E-01 3.85E-01 0.405

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 2 3 4

Mass_mg 6.21 11.8 8.71 8.907

lb/mmBtuO2 1.38E-03 2.63E-03 2.11E-03 0.002

Compound: Hydrogen Fluoride

Average

RunNumber 2 3 4

Mass_mg 8.08 7.65 9.89 8.540

lb/mmBtuO2 1.79E-03 1.71E-03 2.39E-03 0.002

Location: Stack Exit - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.001127 0.000997 0.000577 0.001

lb/mmBtuO2 1.89E-07 1.67E-07 9.43E-08 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.00757 0.00869 0.0033 0.007

Thursday, January 13, 2011 Page 8 of 26
Utility Boiler MACT ICR - Salem Harbor Unit 1

10/1/2010

lb/mmBtuO2 1.27E-06 1.46E-06 5.39E-07 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.0003 0.0003 0.0003 0.000

lb/mmBtuO2 5.03E-08 5.03E-08 4.90E-08 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.000234 0.000244 0.00015 0.000

lb/mmBtuO2 3.93E-08 4.09E-08 2.45E-08 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.003405 0.002803 0.002637 0.003

lb/mmBtuO2 5.71E-07 4.70E-07 4.31E-07 0.000

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.000501 0.000364 0.000336 0.000

lb/mmBtuO2 8.41E-08 6.10E-08 5.49E-08 0.000

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.003724 0.003133 0.002086 0.003

lb/mmBtuO2 6.25E-07 5.25E-07 3.41E-07 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.00472 0.00402 0.00366 0.004

lb/mmBtuO2 7.92E-07 6.74E-07 5.98E-07 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.00714 0.00503 0.00757 0.007

lb/mmBtuO2 1.20E-06 8.43E-07 1.24E-06 0.000

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.2283 0.2938 0.1205 0.214

lb/mmBtuO2 3.83E-05 4.93E-05 1.97E-05 0.000

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Thursday, January 13, 2011 Page 9 of 26
Utility Boiler MACT ICR - Salem Harbor Unit 1

10/1/2010

Process Run Data

Run 1 2 3

lb/mmBtuO2 7.68E-01 7.62E-01 7.57E-01 0.762

ppm 3.29E+02 3.29E+02 3.07E+02 321.667

ppm@7%O2 3.14E+02 3.11E+02 3.09E+02 311.333

Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

lb/mmBtuO2 1.11E-01 1.14E-01 1.17E-01 0.114

ppm 6.64E+01 6.84E+01 6.63E+01 67.033

ppm@7%O2 6.34E+01 6.47E+01 6.68E+01 64.967

Location: Stack Exit - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 1.9 2.4 1 1.767

lb/mmBtuO2 5.20E-04 6.85E-04 2.66E-04 0.000

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 0.5 0.5 0.5 0.500

lb/mmBtuO2 1.37E-04 1.43E-04 1.33E-04 0.000

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 331.41 225.71 274.81 277.310

lb/mmBtuO2 9.07E-02 6.44E-02 7.31E-02 0.076

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 6.19 5.79 10.89 7.623

lb/mmBtuO2 1.69E-03 1.65E-03 2.90E-03 0.002

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 339.5 233.9 286.7 286.700

lb/mmBtuO2 9.29E-02 6.68E-02 7.63E-02 0.079

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 338.1 232 286.2 285.433

lb/mmBtuO2 9.25E-02 6.62E-02 7.61E-02 0.078

Thursday, January 13, 2011 Page 10 of 26
Utility Boiler MACT ICR - Salem Harbor Unit 1

10/1/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

11 Unit Net Electric Generation 39 MW Collected during 

run 2 M0011

0

12 Heat Input 398 Million Btus/hr Collected during 

run 2 Method 10 

and 25A

0

12 CO2 11 % Collected during 

run 2 Method 10 

and 25A

0

12 Steam Output 328 1000 lb steam/hr Collected during 

run 2 Method 10 

and 25A

0

12 Coal Firing Rate 17.5 tons/hr Collected during 

run 2 Method 10 

and 25A

0

12 Urea Flow 38 gph Collected during 

run 2 Method 10 

and 25A

0

12 North O2 10.1 % Collected during 

run 2 Method 10 

and 25A

0

12 South O2 8.4 % Collected during 

run 2 Method 10 

and 25A

0

12 Unit Gross Electrical Output 44 MW Collected during 

run 2 Method 10 

and 25A

0

12 Unit Net Electric Generation 39 MW Collected during 

run 2 Method 10 

and 25A

0

13 Heat Input 399 Million Btus/hr Collected during 

run 3 M0011

0

13 CO2 11 % Collected during 

run 3 M0011

0

13 Steam Output 326 1000 lb steam/hr Collected during 

run 3 M0011

0

13 Coal Firing Rate 17.5 tons/hr Collected during 

run 3 M0011

0

13 Urea Flow 38 gph Collected during 

run 3 M0011

0

13 North O2 10.1 % Collected during 

run 3 M0011

0

13 South O2 8.4 % Collected during 

run 3 M0011

0

Thursday, January 13, 2011 Page 11 of 26
Utility Boiler MACT ICR - Salem Harbor Unit 1

10/1/2010

13 Unit Gross Electrical Output 44 MW Collected during 

run 3 M0011

0

13 Unit Net Electric Generation 38 MW Collected during 

run 3 M0011

0

14 Heat Input 409 Million Btus/hr Collected during 

run 3 Method 10 

and 25A

0

14 CO2 11 % Collected during 

run 3 Method 10 

and 25A

0

14 Steam Output 326 1000 lb steam/hr Collected during 

run 3 Method 10 

and 25A

0

14 Coal Firing Rate 18 tons/hr Collected during 

run 3 Method 10 

and 25A

0

14 Urea Flow 38 gph Collected during 

run 3 Method 10 

and 25A

0

14 North O2 10.1 % Collected during 

run 3 Method 10 

and 25A

0

14 South O2 8.3 % Collected during 

run 3 Method 10 

and 25A

0

14 Unit Gross Electrical Output 44 MW Collected during 

run 3 Method 10 

and 25A

0

14 Unit Net Electric Generation 38 MW Collected during 

run 3 Method 10 

and 25A

0

1 Heat Input 419 Million Btus/hr Collected during 

run 1 OTM 27/28

0

1 CO2 11 % Collected during 

run 1 OTM 27/28

0

1 Steam Output 340 1000 lb steam/hr Collected during 

run 1 OTM 27/28

0

1 Coal Firing Rate 18.5 tons/hr Collected during 

run 1 OTM 27/28

0

1 Urea Flow 52 gph Collected during 

run 1 OTM 27/28

0

1 North O2 10.1 % Collected during 

run 1 OTM 27/28

0

1 South O2 8.6 % Collected during 

run 1 OTM 27/28

0

1 Unit Gross Electrical Output 46 MW Collected during 

run 1 OTM 27/28

0

Thursday, January 13, 2011 Page 12 of 26
Utility Boiler MACT ICR - Salem Harbor Unit 1

10/1/2010

1 Unit Net Electric Generation 41 MW Collected during 

run 1 OTM 27/28

0

2 Heat Input 422 Million Btus/hr Collected during 

run 2 OTM 27/28

0

2 CO2 11 % Collected during 

run 2 OTM 27/28

0

2 Steam Output 346 1000 lb steam/hr Collected during 

run 2 OTM 27/28

0

2 Coal Firing Rate 18.6 tons/hr Collected during 

run 2 OTM 27/28

0

2 Urea Flow 50 gph Collected during 

run 2 OTM 27/28

0

2 North O2 10.1 % Collected during 

run 2 OTM 27/28

0

2 South O2 8.4 % Collected during 

run 2 OTM 27/28

0

2 Unit Gross Electrical Output 47 MW Collected during 

run 2 OTM 27/28

0

2 Unit Net Electric Generation 41 MW Collected during 

run 2 OTM 27/28

0

3 Heat Input 428 Million Btus/hr Collected during 

run 3 OTM 27/28

0

3 CO2 12 % Collected during 

run 3 OTM 27/28

0

3 Steam Output 351 1000 lb steam/hr Collected during 

run 3 OTM 27/28

0

3 Coal Firing Rate 18.8 tons/hr Collected during 

run 3 OTM 27/28

0

3 Urea Flow 43 gph Collected during 

run 3 OTM 27/28

0

3 North O2 10.1 % Collected during 

run 3 OTM 27/28

0

3 South O2 7.3 % Collected during 

run 3 OTM 27/28

0

3 Unit Gross Electrical Output 45 MW Collected during 

run 3 OTM 27/28

0

3 Unit Net Electric Generation 39 MW Collected during 

run 3 OTM 27/28

0

4 Heat Input 420 Million Btus/hr Collected during 

run 1 M29

0

4 CO2 11 % Collected during 

run 1 M29

0

4 Steam Output 343 1000 lb steam/hr Collected during 

run 1 M29

0

4 Coal Firing Rate 18.5 tons/hr Collected during 

run 1 M29

0

Thursday, January 13, 2011 Page 13 of 26
Utility Boiler MACT ICR - Salem Harbor Unit 1

10/1/2010

4 Urea Flow 52 gph Collected during 

run 1 M29

0

4 North O2 10.1 % Collected during 

run 1 M29

0

4 South O2 8.5 % Collected during 

run 1 M29

0

4 Unit Gross Electrical Output 47 MW Collected during 

run 1 M29

0

4 Unit Net Electric Generation 41 MW Collected during 

run 1 M29

0

5 Heat Input 420 Million Btus/hr Collected during 

run 2 M29

0

5 CO2 11 % Collected during 

run 2 M29

0

5 Steam Output 345 1000 lb steam/hr Collected during 

run 2 M29

0

5 Coal Firing Rate 18.5 tons/hr Collected during 

run 2 M29

0

5 Urea Flow 51 gph Collected during 

run 2 M29

0

5 North O2 10.1 % Collected during 

run 2 M29

0

5 South O2 8.5 % Collected during 

run 2 M29

0

5 Unit Gross Electrical Output 47 MW Collected during 

run 2 M29

0

5 Unit Net Electric Generation 41 MW Collected during 

run 2 M29

0

6 Heat Input 426 Million Btus/hr Collected during 

run 3 M29

0

6 CO2 12 % Collected during 

run 3 M29

0

6 Steam Output 365 1000 lb steam/hr Collected during 

run 3 M29

0

6 Coal Firing Rate 18.8 tons/hr Collected during 

run 3 M29

0

6 Urea Flow 43 gph Collected during 

run 3 M29

0

6 North O2 10.1 % Collected during 

run 3 M29

0

6 South O2 6.9 % Collected during 

run 3 M29

0

6 Unit Gross Electrical Output 47 MW Collected during 

run 3 M29

0

6 Unit Net Electric Generation 41 MW Collected during 

run 3 M29

0

Thursday, January 13, 2011 Page 14 of 26
Utility Boiler MACT ICR - Salem Harbor Unit 1

10/1/2010

7 Heat Input 426 Million Btus/hr Collected during 

run 1 M26A, 

Method 7E and 6C

0

7 CO2 12 % Collected during 

run 1 M26A, 

Method 7E and 6C

0

7 Steam Output 339 1000 lb steam/hr Collected during 

run 1 M26A, 

Method 7E and 6C

0

7 Coal Firing Rate 18.8 tons/hr Collected during 

run 1 M26A, 

Method 7E and 6C

0

7 Urea Flow 38 gph Collected during 

run 1 M26A, 

Method 7E and 6C

0

7 North O2 10.1 % Collected during 

run 1 M26A, 

Method 7E and 6C

0

7 South O2 7.6 % Collected during 

run 1 M26A, 

Method 7E and 6C

0

7 Unit Gross Electrical Output 44 MW Collected during 

run 1 M26A, 

Method 7E and 6C

0

7 Unit Net Electric Generation 38 MW Collected during 

run 1 M26A, 

Method 7E and 6C

0

8 Heat Input 425 Million Btus/hr Collected during 

run 2 M26A, 

Method 7E and 6C

0

8 CO2 12 % Collected during 

run 2 M26A, 

Method 7E and 6C

0

8 Steam Output 363 1000 lb steam/hr Collected during 

run 2 M26A, 

Method 7E and 6C

0

8 Coal Firing Rate 18.7 tons/hr Collected during 

run 2 M26A, 

Method 7E and 6C

0

8 Urea Flow 37 gph Collected during 

run 2 M26A, 

Method 7E and 6C

0

8 North O2 10.1 % Collected during 

run 2 M26A, 

Method 7E and 6C

0

8 South O2 6.6 % Collected during 

run 2 M26A, 

Method 7E and 6C

0

Thursday, January 13, 2011 Page 15 of 26
Utility Boiler MACT ICR - Salem Harbor Unit 1

10/1/2010

8 Unit Gross Electrical Output 47 MW Collected during 

run 2 M26A, 

Method 7E and 6C

0

8 Unit Net Electric Generation 41 MW Collected during 

run 2 M26A, 

Method 7E and 6C

0

9 Heat Input 426 Million Btus/hr Collected during 

run 3 M26A, 

Method 7E and 6C

0

9 CO2 12 % Collected during 

run 3 M26A, 

Method 7E and 6C

0

9 Steam Output 362 1000 lb steam/hr Collected during 

run 3 M26A, 

Method 7E and 6C

0

9 Coal Firing Rate 18.7 tons/hr Collected during 

run 3 M26A, 

Method 7E and 6C

0

9 Urea Flow 37 gph Collected during 

run 3 M26A, 

Method 7E and 6C

0

9 North O2 10.1 % Collected during 

run 3 M26A, 

Method 7E and 6C

0

9 South O2 6.6 % Collected during 

run 3 M26A, 

Method 7E and 6C

0

9 Unit Gross Electrical Output 47 MW Collected during 

run 3 M26A, 

Method 7E and 6C

0

9 Unit Net Electric Generation 42 MW Collected during 

run 3 M26A, 

Method 7E and 6C

0

10 Heat Input 402 Million Btus/hr Collected during 

run 1 M0011, 

Method 10 and 

25A

0

10 CO2 11 % Collected during 

run 1 M0011, 

Method 10 and 

25A

0

10 Steam Output 336 1000 lb steam/hr Collected during 

run 1 M0011, 

Method 10 and 

25A

0

10 Coal Firing Rate 17.7 tons/hr Collected during 

run 1 M0011, 

Method 10 and 

25A

0

Thursday, January 13, 2011 Page 16 of 26
Utility Boiler MACT ICR - Salem Harbor Unit 1

10/1/2010

APCD Run Data

Process Lab Run Data

10 Urea Flow 39 gph Collected during 

run 1 M0011, 

Method 10 and 

25A

0

10 North O2 10.1 % Collected during 

run 1 M0011, 

Method 10 and 

25A

0

10 South O2 8.4 % Collected during 

run 1 M0011, 

Method 10 and 

25A

0

10 Unit Gross Electrical Output 46 MW Collected during 

run 1 M0011, 

Method 10 and 

25A

0

10 Unit Net Electric Generation 40 MW Collected during 

run 1 M0011, 

Method 10 and 

25A

0

11 Heat Input 405 Million Btus/hr Collected during 

run 2 M0011

0

11 CO2 11 % Collected during 

run 2 M0011

0

11 Steam Output 331 1000 lb steam/hr Collected during 

run 2 M0011

0

11 Coal Firing Rate 17.8 tons/hr Collected during 

run 2 M0011

0

11 Urea Flow 37 gph Collected during 

run 2 M0011

0

11 North O2 10.1 % Collected during 

run 2 M0011

0

11 South O2 8.3 % Collected during 

run 2 M0011

0

11 Unit Gross Electrical Output 45 MW Collected during 

run 2 M0011

0

Run Name Value UOM Comments

Target

Value

1 LOW NOX BURNERS 0 0

1 SELECTIVE NONCATALYTIC REDUCTION 

FOR NOX

0 0

1 ELECTROSTATIC PRECIPITATOR 0 0

Thursday, January 13, 2011 Page 17 of 26
Utility Boiler MACT ICR - Salem Harbor Unit 1

10/1/2010

Thursday, January 13, 2011 Page 18 of 26
Utility Boiler MACT ICR - Salem Harbor Unit 1

10/1/2010

Sampling / Stack Data Results Detail

Location Stack Exit - Method 0011

Average

Run Number 1 2 3

Test Date 5/7/2010 5/7/2010 5/7/2010

Run Start Time

Run Finish Time

Net Traversing Points 24 24 24

Net Run Time, minutes 120 120 120

Nozzle Diameter, inches 0.259 0.259 0.259 0.259

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9942 0.9942 0.9942 0.994

Barometric Pressure, inches of Mercury 29.82 29.82 29.82 29.820

Average Orifice Meter Differential, inches H2O 2.60 2.56 2.46 2.540

Dry Gas Meter Volume Sampled, cubic feet 105.119 104.938 102.396 104.151

Average Dry Gas Meter Temperature, °F 84.17 90.54 92.73 89.147

Dry Gas Meter Volume Sampled, dscf 101.713 100.353 97.510 99.859

Total Moisture Liquid collected, g 189 191.5 179.8 186.767

Volume of Water Vapor, standard cubic feet 8.90 9.01 8.46 8.790

Moisture Content of Stack Gas, % 8.05 8.24 7.98 8.090

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

Dry Mole Fraction 0.9195 0.9176 0.9202 0.919

Carbon Dioxide, % 10.67 11.101 11.414 11.062

Oxygen, % 9.139 8.645 8.295 8.693

Carbon Monoxide & Nitrogen, % 80.191 80.254 80.291 80.245

Fuel Factor 1.10 1.10 1.10

Dry Molecular Weight, lb/lb-Mole 30.07 30.12 30.16 30.117

Wet Molecular weight, lb/lb-Mole 29.10 29.12 29.19 29.137

Flue Gas Static Pressure, inches of H2O -1.3 -1.3 -1.3 -1.300

Absolute Flue Gas Pressure, inches of Mercury 29.72 29.72 29.72 29.720

Average Stack Gas Temperature, °F 282.88 286.50 289.50 286.293

Average Velocity Head, inches of H2O 0.8536344038

78869

0.839238240

087565

0.808098462

938774

0.834

Average Stack Gas Velocity, feet/second 61.49 61.10 60.00 60.863

Stack Cross-Sectional Area, square feet 63.617 63.617 63.617 63.617

Dry Volumetric Flow Rate, dry scfm 152,364.3 150,352.4 147,471.3 150,062.667

Actual Wet Volumetric Flue Gas Flow Rate, acfm 234,708.6 233,219.9 229,021.2 232,316.567

Percent Isokinetic of Sampling Rate, % 96.7 96.7 95.8 96.400

Percent Excess Air, % 76.0 68.9 64.3 69.733

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

Round Duct Diameter, inches 108 108 108

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 19 of 26
Utility Boiler MACT ICR - Salem Harbor Unit 1

10/1/2010

Location Stack Exit - Method 10

Average

Run Number 1 2 3

Test Date 5/7/2010 5/7/2010 5/7/2010

Run Start Time 10:55:00 AM 4:24:00 PM 6:48:00 PM

Run Finish Time 12:55:00 PM 6:24:00 PM 8:48:00 PM

Carbon Dioxide, % 10.67 11.101 11.414 11.062

Oxygen, % 9.139 8.645 8.295 8.693

Fuel Factor 1.1 1.1 1.1

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

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. 0 0 0 0.000

Calibration Set 1 1 1 1.000

Calibration Pre Zero Cylinder ID CC281576 CC281576 CC281576

Calibration Pre Zero Cylinder Instrument Response 3.04 2.51 2.75 2.767

Calibration Pre Zero Cylinder Bias 1.48 1.21 1.33 1.340

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC91533 CC91533 CC91533

Calibration Pre High Cylinder Instrument Response 95.29 93.7 93.67 94.220

Calibration Pre High Cylinder Bias 1.33 0.54 0.52 0.797

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC281576 CC281576 CC281576

Calibration Post Zero Cylinder Instrument Response 3.37 2.75 2.89 3.003

Calibration Post Zero Cylinder Bias 1.64 1.33 1.4 1.457

Calibration Post Zero Cylinder Drift 0.16 0.12 6.999999999

99998E-02

0.117

Calibration Post High Cylinder ID CC91533 CC91533 CC91533

Calibration Post High Cylinder Instrument Response 92.74 93.67 93.14 93.183

Calibration Post High Cylinder Bias 0.06 0.52 0.26 0.280

Calibration Post High Cylinder Drift 1.27 0.02 0.26 0.517

Cavg 16.64 15.92 15.29 15.950

Cavg Units ppmvd ppmvd ppmvd

Cgas 13.3388 13.1594 12.4115 12.970

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Thursday, January 13, 2011 Page 20 of 26
Utility Boiler MACT ICR - Salem Harbor Unit 1

10/1/2010

Location Stack Exit - Method 25A

Average

Run Number 1 2 3

Test Date 5/7/2010 5/7/2010 5/7/2010

Run Start Time 10:55:00 AM 4:24:00 PM 6:48:00 PM

Run Finish Time 12:55:00 PM 6:24:00 PM 8:48:00 PM

Carbon Dioxide, %

Oxygen, % 9.139 8.645 8.295 8.693

Fuel Factor 0 0 0

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 8.17 8.29 8.16 8.207

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 0 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0 0.000

Calibration Set 2 2 2 2.000

Calibration Pre Zero Cylinder ID CC281576 CC281576 CC281576

Calibration Pre Zero Cylinder Instrument Response 0.017 0.286 0.495 0.266

Calibration Pre Zero Cylinder Bias -1.69 -0.61 0.23 -0.690

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC178755 CC178755 CC178755

Calibration Pre High Cylinder Instrument Response 6.764 7.29 7.301 7.118

Calibration Pre High Cylinder Bias -0.84 1.27 1.32 0.583

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC281576 CC281576 CC281576

Calibration Post Zero Cylinder Instrument Response 0.227 0.495 0.255 0.326

Calibration Post Zero Cylinder Bias -0.85 0.23 -0.74 -0.453

Calibration Post Zero Cylinder Drift 0.84 0.84 0.97 0.883

Calibration Post High Cylinder ID CC178755 CC178755 CC178755

Calibration Post High Cylinder Instrument Response 6.673 7.301 6.875 6.950

Calibration Post High Cylinder Bias -1.21 1.32 -0.4 -0.097

Calibration Post High Cylinder Drift 0.37 0.05 1.72 0.713

Cavg 0.272 0.89 0.682 0.615

Cavg Units ppmvw ppmvw ppmvw

Cgas 0.1734 0.5522 0.3486 0.358

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0.1591980595

77048

0.506444532

94714

0.320170862

505586

0.329

Cgasw Units ppmvw ppmvw ppmvw

Thursday, January 13, 2011 Page 21 of 26
Utility Boiler MACT ICR - Salem Harbor Unit 1

10/1/2010

Location Stack Exit - Method 26A

Average

Run Number 2 3 4

Test Date 5/6/2010 5/6/2010 5/6/2010

Run Start Time

Run Finish Time

Net Traversing Points 36 36 36

Net Run Time, minutes 180 180 180

Nozzle Diameter, inches 0.259 0.259 0.259 0.259

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9965 0.9965 0.9965 0.997

Barometric Pressure, inches of Mercury 29.57 29.35 29.35 29.423

Average Orifice Meter Differential, inches H2O 2.20 2.12 2.03 2.117

Dry Gas Meter Volume Sampled, cubic feet 146.243 146.239 143.974 145.485

Average Dry Gas Meter Temperature, °F 88.93 92.57 93.69 91.730

Dry Gas Meter Volume Sampled, dscf 139.293 137.320 134.890 137.168

Total Moisture Liquid collected, g 394 425 368.4 395.800

Volume of Water Vapor, standard cubic feet 18.55 20.00 17.34 18.630

Moisture Content of Stack Gas, % 11.75 12.71 11.39 11.950

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

Dry Mole Fraction 0.8825 0.8729 0.8861 0.881

Carbon Dioxide, % 13.1 13.2 12.5 12.933

Oxygen, % 6.3 6.2 7.1 6.533

Carbon Monoxide & Nitrogen, % 80.6 80.6 80.4 80.533

Fuel Factor 1.11 1.11 1.10

Dry Molecular Weight, lb/lb-Mole 30.35 30.36 30.28 30.330

Wet Molecular weight, lb/lb-Mole 28.90 28.79 28.88 28.857

Flue Gas Static Pressure, inches of H2O -1.1 -1.25 -1.4 -1.250

Absolute Flue Gas Pressure, inches of Mercury 29.49 29.26 29.25 29.333

Average Stack Gas Temperature, °F 290.33 294.94 295.08 293.450

Average Velocity Head, inches of H2O 0.7209317239

14294

0.701715916

222428

0.668541599

004948

0.697

Average Stack Gas Velocity, feet/second 57.21 56.95 55.51 56.557

Stack Cross-Sectional Area, square feet 63.617 63.617 63.617 63.617

Dry Volumetric Flow Rate, dry scfm 133,661.4 129,782.7 128,346.4 130,596.833

Actual Wet Volumetric Flue Gas Flow Rate, acfm 218,371.7 217,379.3 211,882.8 215,877.933

Percent Isokinetic of Sampling Rate, % 100.7 102.2 101.5 101.467

Percent Excess Air, % 42.1 41.1 50.3 44.500

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

Round Duct Diameter, inches 108 108 108

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 22 of 26
Utility Boiler MACT ICR - Salem Harbor Unit 1

10/1/2010

Location Stack Exit - Method 29

Average

Run Number 1 2 3

Test Date 5/4/2010 5/4/2010 5/5/2010

Run Start Time

Run Finish Time

Net Traversing Points 48 48 48

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.258 0.258 0.258 0.258

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9965 0.9965 0.9965 0.997

Barometric Pressure, inches of Mercury 29.8 29.8 30 29.867

Average Orifice Meter Differential, inches H2O 2.69 2.81 2.38 2.627

Dry Gas Meter Volume Sampled, cubic feet 216.605 221.617 201.608 213.277

Average Dry Gas Meter Temperature, °F 93.06 98.91 91.46 94.477

Dry Gas Meter Volume Sampled, dscf 206.602 209.232 193.995 203.276

Total Moisture Liquid collected, g 402.9 432 419 417.967

Volume of Water Vapor, standard cubic feet 18.96 20.33 19.72 19.670

Moisture Content of Stack Gas, % 8.41 8.86 9.23 8.833

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

Dry Mole Fraction 0.9159 0.9114 0.9077 0.912

Carbon Dioxide, % 11.746 11.61 12.857 12.071

Oxygen, % 7.899 8.052 6.685 7.545

Carbon Monoxide & Nitrogen, % 80.355 80.338 80.458 80.384

Fuel Factor 1.11 1.11 1.11

Dry Molecular Weight, lb/lb-Mole 30.20 30.18 30.32 30.233

Wet Molecular weight, lb/lb-Mole 29.17 29.10 29.18 29.150

Flue Gas Static Pressure, inches of H2O -0.85 -0.85 -0.85 -0.850

Absolute Flue Gas Pressure, inches of Mercury 29.74 29.74 29.94 29.807

Average Stack Gas Temperature, °F 296.56 300.48 289.15 295.397

Average Velocity Head, inches of H2O 0.8739484012

56162

0.918331511

80871

0.774138397

857432

0.855

Average Stack Gas Velocity, feet/second 62.69 64.51 58.51 61.903

Stack Cross-Sectional Area, square feet 63.617 63.617 63.617 63.617

Dry Volumetric Flow Rate, dry scfm 152,034.0 154,876.7 142,972.4 149,961.033

Actual Wet Volumetric Flue Gas Flow Rate, acfm 239,289.0 246,236.0 223,333.8 236,286.267

Percent Isokinetic of Sampling Rate, % 99.2 98.6 99.1 98.967

Percent Excess Air, % 59.3 61.2 45.9 55.467

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

Round Duct Diameter, inches 108 108 108

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 26
Utility Boiler MACT ICR - Salem Harbor Unit 1

10/1/2010

Location Stack Exit - Method 6C

Average

Run Number 1 2 3

Test Date 5/6/2010 5/6/2010 5/6/2010

Run Start Time 7:01:00 AM 10:18:00 AM 2:25:00 PM

Run Finish Time 10:01:00 AM 1:18:00 PM 5:25:00 PM

Carbon Dioxide, % 13.13 13.229 12.47 12.943

Oxygen, % 6.342 6.208 7.11 6.553

Fuel Factor 1.11 1.11 1.11

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

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. 0 0 0 0.000

Calibration Set 3 3 3 3.000

Calibration Pre Zero Cylinder ID CC281576 CC281576 CC281576

Calibration Pre Zero Cylinder Instrument Response 5.05 13.61 12.41 10.357

Calibration Pre Zero Cylinder Bias 0.97 2.88 2.61 2.153

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC301684 CC301684 CC301684

Calibration Pre High Cylinder Instrument Response 443.49 445.03 443.76 444.093

Calibration Pre High Cylinder Bias -1.77 -1.43 -1.71 -1.637

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC281576 CC281576 CC281576

Calibration Post Zero Cylinder Instrument Response 13.61 12.41 19.38 15.133

Calibration Post Zero Cylinder Bias 2.88 2.61 4.16 3.217

Calibration Post Zero Cylinder Drift 1.91 0.27 1.55 1.243

Calibration Post High Cylinder ID CC301684 CC301684 CC301684

Calibration Post High Cylinder Instrument Response 445.03 443.76 437.22 442.003

Calibration Post High Cylinder Bias -1.43 -1.71 -3.17 -2.103

Calibration Post High Cylinder Drift 0.34 0.28 1.46 0.693

Cavg 327.76 329.15 306.22 321.043

Cavg Units ppmvd ppmvd ppmvd

Cgas 329.0241 329.3423 307.2859 321.884

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Thursday, January 13, 2011 Page 24 of 26
Utility Boiler MACT ICR - Salem Harbor Unit 1

10/1/2010

Location Stack Exit - Method 7E

Average

Run Number 1 2 3

Test Date 5/6/2010 5/6/2010 5/6/2010

Run Start Time 7:01:00 AM 10:18:00 AM 2:25:00 PM

Run Finish Time 10:01:00 AM 1:18:00 PM 5:25:00 PM

Carbon Dioxide, % 13.13 13.229 12.47 12.943

Oxygen, % 6.342 6.208 7.11 6.553

Fuel Factor 1.11 1.11 1.11

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

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. 0 0 0 0.000

Calibration Set 4 4 4 4.000

Calibration Pre Zero Cylinder ID CC281576 CC281576 CC281576

Calibration Pre Zero Cylinder Instrument Response 0.14 0.02 0.03 0.063

Calibration Pre Zero Cylinder Bias 0.12 0.05 0.06 0.077

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID SG914537 SG914537 SG914537

Calibration Pre High Cylinder Instrument Response 88.08 88.49 88.42 88.330

Calibration Pre High Cylinder Bias -1.6 -1.38 -1.42 -1.467

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC281576 CC281576 CC281576

Calibration Post Zero Cylinder Instrument Response 0.02 0.03 0.36 0.137

Calibration Post Zero Cylinder Bias 0.05 0.06 0.24 0.117

Calibration Post Zero Cylinder Drift 0.07 0.01 0.18 0.087

Calibration Post High Cylinder ID SG914537 SG914537 SG914537

Calibration Post High Cylinder Instrument Response 88.49 88.42 88.7 88.537

Calibration Post High Cylinder Bias -1.38 -1.42 -1.27 -1.357

Calibration Post High Cylinder Drift 0.22 0.04 0.15 0.137

Cavg 64.35 66.43 64.5 65.093

Cavg Units ppmvd ppmvd ppmvd

Cgas 66.3649 68.395 66.2808 67.014

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Thursday, January 13, 2011 Page 25 of 26
Utility Boiler MACT ICR - Salem Harbor Unit 1

10/1/2010

Location Stack Exit - OTM - 27/28

Average

Run Number 1 2 3

Test Date 5/4/2010 5/4/2010 5/5/2010

Run Start Time

Run Finish Time

Net Traversing Points 12 12 12

Net Run Time, minutes 345.25 330.75 308.75

Nozzle Diameter, inches 0.175 0.175 0.175 0.175

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 29.6 29.25 29.8 29.550

Average Orifice Meter Differential, inches H2O 0.44 0.45 0.47 0.453

Dry Gas Meter Volume Sampled, cubic feet 136.645 135.638 125.908 132.730

Average Dry Gas Meter Temperature, °F 97.08 103.17 89.25 96.500

Dry Gas Meter Volume Sampled, dscf 126.638 122.880 119.158 122.892

Total Moisture Liquid collected, g 263.3 252.7 250 255.333

Volume of Water Vapor, standard cubic feet 12.39 11.89 11.77 12.017

Moisture Content of Stack Gas, % 8.91 8.82 8.99 8.907

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

Dry Mole Fraction 0.9109 0.9118 0.9101 0.911

Carbon Dioxide, % 11.75 11.61 12.86 12.073

Oxygen, % 7.899 8.052 6.685 7.545

Carbon Monoxide & Nitrogen, % 80.351 80.338 80.455 80.381

Fuel Factor 1.11 1.11 1.11

Dry Molecular Weight, lb/lb-Mole 30.20 30.18 30.33 30.237

Wet Molecular weight, lb/lb-Mole 29.11 29.11 29.22 29.147

Flue Gas Static Pressure, inches of H2O -0.85 -0.85 -0.85 -0.850

Absolute Flue Gas Pressure, inches of Mercury 29.54 29.19 29.74 29.490

Average Stack Gas Temperature, °F 295.08 299.92 288.33 294.443

Average Velocity Head, inches of H2O 0.8903323267

87942

0.898311843

64841

0.789136987

280673

0.859

Average Stack Gas Velocity, feet/second 63.50 64.37 59.20 62.357

Stack Cross-Sectional Area, square feet 63.617 63.617 63.617 63.617

Dry Volumetric Flow Rate, dry scfm 152,425.9 151,860.9 144,229.9 149,505.567

Actual Wet Volumetric Flue Gas Flow Rate, acfm 242,380.8 245,701.6 225,967.6 238,016.667

Percent Isokinetic of Sampling Rate, % 91.7 93.2 101.9 95.600

Percent Excess Air, % 59.3 61.2 45.9 55.467

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

Round Duct Diameter, inches 108 108 108

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 26 of 26