Name: David Nuckols

Title: Manager F&H Operations

Company: Dominion Generation

Sign Date:

Name: Michael P. Martin

Title: Senior Project Manager

Company: TRC Companies, Inc.

Sign Date:

Permitted Facility Representative / Date Testing Company Representative / Date

Utility Boiler MACT ICR - Clover Power Station Unit 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.

Wednesday, January 12, 2011 Page 1 of 27
Utility Boiler MACT ICR - Clover Power Station Unit 2

Facility Information:

Clover

P.O. Box 245

Route 92

Clover VA 24534

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:

7213

Permitted Source ID/Name:

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:

5100 mmBtu/hr tangentially fired, pulverized coal boiler with LNB w/ overfire air, SNCR, wet limestone FGD, & 

baghouse.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 5108300046 FRS #: 110007008175

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 267 0 0 0 1012 2682 4 6

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Exit Carbon Monoxide Method 10 6 180 0

Stack Exit Formaldehyde Method 0011 5 120 0

Total organic compounds 

(TOC) as Propane

Method 25A 6 180 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

Wednesday, January 12, 2011 Page 2 of 27
Utility Boiler MACT ICR - Clover Power Station Unit 2

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.

Stack Exit Selenium Method 29 3 240 0

Stack Exit Antimony Method 29 3 240 0

Stack Exit Arsenic Method 29 3 240 0

Stack Exit Beryllium Method 29 3 240 0

Stack Exit Cadmium Method 29 3 240 0

Stack Exit Cobalt Method 29 3 240 0

Stack Exit Chromium 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

Inorganic (Aqueous) 

Condensible Part.

Stack Exit Method 5/OTM-28 3 240 0

Organic Condensible 

Particulate

Stack Exit Method 5/OTM-28 3 240 0

Stack Exit Total Particulate Method 5/OTM-28 3 240 0

Stack Exit Filterable Particulate Method 5/OTM-28 3 240 0

Stack Exit Sulfur Dioxide Method 6C 6 180 0

Stack Exit Nitrogen oxides (NOx) Method 7E 6 180 0

Wednesday, January 12, 2011 Page 3 of 27
Utility Boiler MACT ICR - Clover Power Station Unit 2

Sampling / Stack Data Results Summary

Location Stack Exit - Method 0011

Average

Run Number 3 4 5

Test Date 3/30/2010 3/31/2010 4/2/2010

Run Start Time

Run Finish Time

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 91.182 91.284 85.263 89.243

Moisture Content of Stack Gas, % 13.06 12.97 13.13 13.053

Moisture Saturation at Stack Gas Temperature, % 12.95 12.56 12.73 12.747

Carbon Dioxide, % 13.21 13.211 13.266 13.229

Oxygen, % 5.912 5.941 5.914 5.922

Average Stack Gas Temperature, °F 123.29 122.38 123.13 122.933

Dry Volumetric Flow Rate, dry scfm 1,158,936.3 1,161,687.3 1,083,818.1 1,134,813.90

0

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,512,202.6 1,498,438.4 1,392,056.9 1,467,565.96

7

Percent Isokinetic of Sampling Rate, % 98.4 98.2 99.2 98.600

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

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

Wednesday, January 12, 2011 Page 4 of 27
Utility Boiler MACT ICR - Clover Power Station Unit 2

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

Wednesday, January 12, 2011 Page 5 of 27
Utility Boiler MACT ICR - Clover Power Station Unit 2

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 5/OTM-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

Wednesday, January 12, 2011 Page 6 of 27
Utility Boiler MACT ICR - Clover Power Station Unit 2

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

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

Wednesday, January 12, 2011 Page 7 of 27
Utility Boiler MACT ICR - Clover Power Station Unit 2

Emissions Summary

Location: Stack Exit - Method 0011

Compound: Formaldehyde

Average

RunNumber 3 4 5

Mass_mg 0.0157 0.0256 0.0199 0.020

lb/mmBtuO2 5.18E-06 8.45E-06 7.02E-06 0.000

ppm 4.87E-03 7.93E-03 6.60E-03 0.006

ppm@7%O2 4.52E-03 7.37E-03 6.12E-03 0.006

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 3 4 5

lb/mmBtuO2 4.94E-02 6.76E-02 2.64E-02 0.048

ppm 4.98E+01 6.81E+01 2.66E+01 48.167

ppm@7%O2 4.62E+01 6.33E+01 2.47E+01 44.733

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 3 4 5

lb/mmBtuO2 7.37E-05 1.19E-05 3.00E-05 0.000

ppm 4.94E-02 7.60E-03 2.01E-02 0.026

ppm@7%O2 4.38E-02 7.06E-03 1.78E-02 0.023

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 1.46 1.9 1.49 1.617

lb/mmBtuO2 3.00E-04 3.95E-04 3.18E-04 0.000

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.853 0.874 0.934 0.887

lb/mmBtuO2 1.75E-04 1.82E-04 1.99E-04 0.000

Location: Stack Exit - Method 29 

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.00125 0.000671 0.000454 0.001

lb/mmBtuO2 2.02E-07 1.09E-07 7.56E-08 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.00143 0.00101 0.00441 0.002

Wednesday, January 12, 2011 Page 8 of 27
Utility Boiler MACT ICR - Clover Power Station Unit 2

lb/mmBtuO2 2.32E-07 1.65E-07 7.34E-07 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.0002 0.0002 0.0002 0.000

lb/mmBtuO2 3.24E-08 3.26E-08 3.33E-08 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.000379 0.000127 0.0001 0.000

lb/mmBtuO2 6.14E-08 2.07E-08 1.67E-08 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.062 0.0227 0.00752 0.031

lb/mmBtuO2 1.00E-05 3.70E-06 1.25E-06 0.000

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.00148 0.000933 0.000335 0.001

lb/mmBtuO2 2.40E-07 1.52E-07 5.58E-08 0.000

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.00231 0.00142 0.00144 0.002

lb/mmBtuO2 3.74E-07 2.31E-07 2.40E-07 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.124 0.107 0.0557 0.096

lb/mmBtuO2 2.01E-05 1.74E-05 9.28E-06 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.0577 0.0206 0.00893 0.029

lb/mmBtuO2 9.34E-06 3.36E-06 1.49E-06 0.000

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.0152 0.0201 0.134 0.056

lb/mmBtuO2 2.46E-06 3.28E-06 2.23E-05 0.000

Location: Stack Exit - Method 5/OTM-28

Compound: Filterable Particulate

Average

Wednesday, January 12, 2011 Page 9 of 27
Utility Boiler MACT ICR - Clover Power Station Unit 2

Process Run Data

RunNumber 1 2 3

Mass_mg 6.3 18.6 20.3 15.067

lb/mmBtuO2 1.05E-03 3.13E-03 3.46E-03 0.003

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 9 26.7 8.8 14.833

lb/mmBtuO2 1.51E-03 4.49E-03 1.50E-03 0.003

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 1.4 1.8 1.6 1.600

lb/mmBtuO2 2.34E-04 3.03E-04 2.73E-04 0.000

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 14.7 45.1 28.7 29.500

lb/mmBtuO2 2.46E-03 7.58E-03 4.89E-03 0.005

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

lb/mmBtuO2 5.87E-02 9.61E-02 8.27E-02 0.079

ppm 2.71E+01 4.24E+01 3.64E+01 35.300

ppm@7%O2 2.40E+01 3.93E+01 3.39E+01 32.400

Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

lb/mmBtuO2 2.86E-01 3.36E-01 3.28E-01 0.317

ppm 1.84E+02 2.06E+02 2.01E+02 197.000

ppm@7%O2 1.63E+02 1.91E+02 1.87E+02 180.333

Wednesday, January 12, 2011 Page 10 of 27
Utility Boiler MACT ICR - Clover Power Station Unit 2

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input 4548.3 Million Btus/hr Collected during 

M26A run 1

0

1 Steam Output 3274.1 1000 lb steam/hr Collected during 

M26A run 1

0

1 Fuel Oil Firing Rate 0 gal/hr Collected during 

M26A run 1

0

1 Flue Gas Flow Rate 1E+06 dscfm Collected during 

M26A run 1

0

1 Pressure Drop Across FGD 2.49 in H20 Collected during 

M26A run 1

0

1 FGD Scrubber Liquor Flow Rate 152486 gal/min Collected during 

M26A run 1

0

1 Coal Firing Rate 174.51 tons/day Collected during 

M26A run 1

0

1 Flue Gas Carbon Dioxide Content 12.53 % Collected during 

M26A run 1

0

1 Flue Gas Sampling Point Temperature 128.58 Deg F Collected during 

M26A run 1

0

1 Unit Gross Electrical Output 464.67 Mwe Collected during 

M26A run 1

0

1 Unit Net Electric Generation 433.93 MWh Collected during 

M26A run 1

0

2 Heat Input 4541.7 Million Btus/hr Collected during 

Method 6C and 7E 

run 1

0

2 Steam Output 3277.3 1000 lb steam/hr Collected during 

Method 6C and 7E 

run 1

0

2 Fuel Oil Firing Rate 0 gal/hr Collected during 

Method 6C and 7E 

run 1

0

2 Flue Gas Flow Rate 1E+06 dscfm Collected during 

Method 6C and 7E 

run 1

0

2 Pressure Drop Across FGD 2.49 in H20 Collected during 

Method 6C and 7E 

run 1

0

2 FGD Scrubber Liquor Flow Rate 152486 gal/min Collected during 

Method 6C and 7E 

run 1

0

2 Coal Firing Rate 174.14 tons/day Collected during 

Method 6C and 7E 

run 1

0

Wednesday, January 12, 2011 Page 11 of 27
Utility Boiler MACT ICR - Clover Power Station Unit 2

2 Flue Gas Carbon Dioxide Content 12.54 % Collected during 

Method 6C and 7E 

run 1

0

2 Flue Gas Sampling Point Temperature 128.45 Deg F Collected during 

Method 6C and 7E 

run 1

0

2 Unit Gross Electrical Output 465 Mwe Collected during 

Method 6C and 7E 

run 1

0

2 Unit Net Electric Generation 434.71 MWh Collected during 

Method 6C and 7E 

run 1

0

3 Heat Input 4565.3 Million Btus/hr Collected during 

run 2 of M26A, 

run 2 of Method 

6C and 7E, run 3 

of M0011, and run 

3 of Method 10 

and 25A

0

3 Steam Output 3260.9 1000 lb steam/hr Collected during 

run 2 of M26A, 

run 2 of Method 

6C and 7E, run 3 

of M0011, and run 

3 of Method 10 

and 25A

0

3 Fuel Oil Firing Rate 0 gal/hr Collected during 

run 2 of M26A, 

run 2 of Method 

6C and 7E, run 3 

of M0011, and run 

3 of Method 10 

and 25A

0

3 Flue Gas Flow Rate 1E+06 dscfm Collected during 

run 2 of M26A, 

run 2 of Method 

6C and 7E, run 3 

of M0011, and run 

3 of Method 10 

and 25A

0

3 Pressure Drop Across FGD 2.46 in H20 Collected during 

run 2 of M26A, 

run 2 of Method 

6C and 7E, run 3 

of M0011, and run 

3 of Method 10 

and 25A

0

Wednesday, January 12, 2011 Page 12 of 27
Utility Boiler MACT ICR - Clover Power Station Unit 2

3 FGD Scrubber Liquor Flow Rate 152486 gal/min Collected during 

run 2 of M26A, 

run 2 of Method 

6C and 7E, run 3 

of M0011, and run 

3 of Method 10 

and 25A

0

3 Coal Firing Rate 178.46 tons/day Collected during 

run 2 of M26A, 

run 2 of Method 

6C and 7E, run 3 

of M0011, and run 

3 of Method 10 

and 25A

0

3 Flue Gas Carbon Dioxide Content 12.03 % Collected during 

run 2 of M26A, 

run 2 of Method 

6C and 7E, run 3 

of M0011, and run 

3 of Method 10 

and 25A

0

3 Flue Gas Sampling Point Temperature 128.44 Deg F Collected during 

run 2 of M26A, 

run 2 of Method 

6C and 7E, run 3 

of M0011, and run 

3 of Method 10 

and 25A

0

3 Unit Gross Electrical Output 460.67 Mwe Collected during 

run 2 of M26A, 

run 2 of Method 

6C and 7E, run 3 

of M0011, and run 

3 of Method 10 

and 25A

0

3 Unit Net Electric Generation 428.47 MWh Collected during 

run 2 of M26A, 

run 2 of Method 

6C and 7E, run 3 

of M0011, and run 

3 of Method 10 

and 25A

0

4 Heat Input 4555.7 Million Btus/hr Collected during 

M26A run 3

0

4 Steam Output 3293.1 1000 lb steam/hr Collected during 

M26A run 3

0

4 Fuel Oil Firing Rate 0 gal/hr Collected during 

M26A run 3

0

4 Flue Gas Flow Rate 1E+06 dscfm Collected during 

M26A run 3

0

Wednesday, January 12, 2011 Page 13 of 27
Utility Boiler MACT ICR - Clover Power Station Unit 2

4 Pressure Drop Across FGD 2.45 in H20 Collected during 

M26A run 3

0

4 FGD Scrubber Liquor Flow Rate 152486 gal/min Collected during 

M26A run 3

0

4 Coal Firing Rate 179.59 tons/day Collected during 

M26A run 3

0

4 Flue Gas Carbon Dioxide Content 11.89 % Collected during 

M26A run 3

0

4 Flue Gas Sampling Point Temperature 128.19 Deg F Collected during 

M26A run 3

0

4 Unit Gross Electrical Output 466.75 Mwe Collected during 

M26A run 3

0

4 Unit Net Electric Generation 435.33 MWh Collected during 

M26A run 3

0

5 Heat Input 4558.2 Million Btus/hr Collected during 

run 3 of Method 

6C and 7E

0

5 Steam Output 3290.5 1000 lb steam/hr Collected during 

run 3 of Method 

6C and 7E

0

5 Fuel Oil Firing Rate 0 gal/hr Collected during 

run 3 of Method 

6C and 7E

0

5 Flue Gas Flow Rate 1E+06 dscfm Collected during 

run 3 of Method 

6C and 7E

0

5 Pressure Drop Across FGD 2.47 in H20 Collected during 

run 3 of Method 

6C and 7E

0

5 FGD Scrubber Liquor Flow Rate 152486 gal/min Collected during 

run 3 of Method 

6C and 7E

0

5 Coal Firing Rate 180.04 tons/day Collected during 

run 3 of Method 

6C and 7E

0

5 Flue Gas Carbon Dioxide Content 11.88 % Collected during 

run 3 of Method 

6C and 7E

0

5 Flue Gas Sampling Point Temperature 128.05 Deg F Collected during 

run 3 of Method 

6C and 7E

0

5 Unit Gross Electrical Output 467.33 Mwe Collected during 

run 3 of Method 

6C and 7E

0

5 Unit Net Electric Generation 435.42 MWh Collected during 

run 3 of Method 

6C and 7E

0

Wednesday, January 12, 2011 Page 14 of 27
Utility Boiler MACT ICR - Clover Power Station Unit 2

6 Heat Input 4561.4 Million Btus/hr Collected during 

run 4 of M0011 

and run 4 of 

Method 10 and 

25A

0

6 Steam Output 3286.5 1000 lb steam/hr Collected during 

run 4 of M0011 

and run 4 of 

Method 10 and 

25A

0

6 Fuel Oil Firing Rate 0 gal/hr Collected during 

run 4 of M0011 

and run 4 of 

Method 10 and 

25A

0

6 Flue Gas Flow Rate 1E+06 dscfm Collected during 

run 4 of M0011 

and run 4 of 

Method 10 and 

25A

0

6 Pressure Drop Across FGD 2.39 in H20 Collected during 

run 4 of M0011 

and run 4 of 

Method 10 and 

25A

0

6 FGD Scrubber Liquor Flow Rate 152486 gal/min Collected during 

run 4 of M0011 

and run 4 of 

Method 10 and 

25A

0

6 Coal Firing Rate 173.79 tons/day Collected during 

run 4 of M0011 

and run 4 of 

Method 10 and 

25A

0

6 Flue Gas Carbon Dioxide Content 11.9 % Collected during 

run 4 of M0011 

and run 4 of 

Method 10 and 

25A

0

6 Flue Gas Sampling Point Temperature 127.95 Deg F Collected during 

run 4 of M0011 

and run 4 of 

Method 10 and 

25A

0

6 Unit Gross Electrical Output 465.5 Mwe Collected during 

run 4 of M0011 

and run 4 of 

Method 10 and 

25A

0

Wednesday, January 12, 2011 Page 15 of 27
Utility Boiler MACT ICR - Clover Power Station Unit 2

6 Unit Net Electric Generation 434.38 MWh Collected during 

run 4 of M0011 

and run 4 of 

Method 10 and 

25A

0

7 Heat Input 4281.5 Million Btus/hr Collected during 

M0011 run 5

0

7 Steam Output 3075.1 1000 lb steam/hr Collected during 

M0011 run 5

0

7 Fuel Oil Firing Rate 0 gal/hr Collected during 

M0011 run 5

0

7 Flue Gas Flow Rate 1E+06 dscfm Collected during 

M0011 run 5

0

7 Pressure Drop Across FGD 2.54 in H20 Collected during 

M0011 run 5

0

7 FGD Scrubber Liquor Flow Rate 152486 gal/min Collected during 

M0011 run 5

0

7 Coal Firing Rate 163.23 tons/day Collected during 

M0011 run 5

0

7 Flue Gas Carbon Dioxide Content 11.94 % Collected during 

M0011 run 5

0

7 Flue Gas Sampling Point Temperature 128.53 Deg F Collected during 

M0011 run 5

0

7 Unit Gross Electrical Output 437 Mwe Collected during 

M0011 run 5

0

7 Unit Net Electric Generation 406.19 MWh Collected during 

M0011 run 5

0

8 Heat Input 4306.2 Million Btus/hr Collected during 

run 5 of Method 

10 and 25A

0

8 Steam Output 3075.0 1000 lb steam/hr Collected during 

run 5 of Method 

10 and 25A

0

8 Fuel Oil Firing Rate 0 gal/hr Collected during 

run 5 of Method 

10 and 25A

0

8 Flue Gas Flow Rate 1E+06 dscfm Collected during 

run 5 of Method 

10 and 25A

0

8 Pressure Drop Across FGD 2.48 in H20 Collected during 

run 5 of Method 

10 and 25A

0

8 FGD Scrubber Liquor Flow Rate 152486 gal/min Collected during 

run 5 of Method 

10 and 25A

0

8 Coal Firing Rate 163.06 tons/day Collected during 

run 5 of Method 

10 and 25A

0

Wednesday, January 12, 2011 Page 16 of 27
Utility Boiler MACT ICR - Clover Power Station Unit 2

8 Flue Gas Carbon Dioxide Content 11.95 % Collected during 

run 5 of Method 

10 and 25A

0

8 Flue Gas Sampling Point Temperature 129.6 Deg F Collected during 

run 5 of Method 

10 and 25A

0

8 Unit Gross Electrical Output 437 Mwe Collected during 

run 5 of Method 

10 and 25A

0

8 Unit Net Electric Generation 406.45 MWh Collected during 

run 5 of Method 

10 and 25A

0

9 Heat Input 4363.8 Million Btus/hr Collected during 

M29 and 

M5/OTM28 run 1

0

9 Steam Output 3201 1000 lb steam/hr Collected during 

M29 and 

M5/OTM28 run 1

0

9 Fuel Oil Firing Rate 0 gal/hr Collected during 

M29 and 

M5/OTM28 run 1

0

9 Flue Gas Flow Rate 1E+06 dscfm Collected during 

M29 and 

M5/OTM28 run 1

0

9 Pressure Drop Across FGD 2.46 in H20 Collected during 

M29 and 

M5/OTM28 run 1

0

9 FGD Scrubber Liquor Flow Rate 152486 gal/min Collected during 

M29 and 

M5/OTM28 run 1

0

9 Coal Firing Rate 170.28 tons/day Collected during 

M29 and 

M5/OTM28 run 1

0

9 Flue Gas Carbon Dioxide Content 11.9 % Collected during 

M29 and 

M5/OTM28 run 1

0

9 Flue Gas Sampling Point Temperature 127.93 Deg F Collected during 

M29 and 

M5/OTM28 run 1

0

9 Unit Gross Electrical Output 448.8 Mwe Collected during 

M29 and 

M5/OTM28 run 1

0

9 Unit Net Electric Generation 423.93 MWh Collected during 

M29 and 

M5/OTM28 run 1

0

10 Heat Input 4274 Million Btus/hr Collected during 

M29 and 

M5/OTM28 run 2

0

Wednesday, January 12, 2011 Page 17 of 27
Utility Boiler MACT ICR - Clover Power Station Unit 2

10 Steam Output 3087.6 1000 lb steam/hr Collected during 

M29 and 

M5/OTM28 run 2

0

10 Fuel Oil Firing Rate 0 gal/hr Collected during 

M29 and 

M5/OTM28 run 2

0

10 Flue Gas Flow Rate 1E+06 dscfm Collected during 

M29 and 

M5/OTM28 run 2

0

10 Pressure Drop Across FGD 2.45 in H20 Collected during 

M29 and 

M5/OTM28 run 2

0

10 FGD Scrubber Liquor Flow Rate 152486 gal/min Collected during 

M29 and 

M5/OTM28 run 2

0

10 Coal Firing Rate 161.37 tons/day Collected during 

M29 and 

M5/OTM28 run 2

0

10 Flue Gas Carbon Dioxide Content 12.05 % Collected during 

M29 and 

M5/OTM28 run 2

0

10 Flue Gas Sampling Point Temperature 128.63 Deg F Collected during 

M29 and 

M5/OTM28 run 2

0

10 Unit Gross Electrical Output 437.2 Mwe Collected during 

M29 and 

M5/OTM28 run 2

0

10 Unit Net Electric Generation 406.96 MWh Collected during 

M29 and 

M5/OTM28 run 2

0

11 Heat Input 4380.2 Million Btus/hr Collected during 

M29 and 

M5/OTM28 run 3

0

11 Steam Output 3080.5 1000 lb steam/hr Collected during 

M29 and 

M5/OTM28 run 3

0

11 Fuel Oil Firing Rate 0 gal/hr Collected during 

M29 and 

M5/OTM28 run 3

0

11 Flue Gas Flow Rate 1E+06 dscfm Collected during 

M29 and 

M5/OTM28 run 3

0

11 Pressure Drop Across FGD 2.44 in H20 Collected during 

M29 and 

M5/OTM28 run 3

0

11 FGD Scrubber Liquor Flow Rate 152486 gal/min Collected during 

M29 and 

M5/OTM28 run 3

0

Wednesday, January 12, 2011 Page 18 of 27
Utility Boiler MACT ICR - Clover Power Station Unit 2

APCD Run Data

Process Lab Run Data

11 Coal Firing Rate 163.51 tons/day Collected during 

M29 and 

M5/OTM28 run 3

0

11 Flue Gas Carbon Dioxide Content 11.88 % Collected during 

M29 and 

M5/OTM28 run 3

0

11 Flue Gas Sampling Point Temperature 130.78 Deg F Collected during 

M29 and 

M5/OTM28 run 3

0

11 Unit Gross Electrical Output 442.67 Mwe Collected during 

M29 and 

M5/OTM28 run 3

0

11 Unit Net Electric Generation 407.31 MWh Collected during 

M29 and 

M5/OTM28 run 3

0

Run Name Value UOM Comments

Target

Value

1 LOW NOX BURNERS 0 0

1 OVERFIRE AIR 0 0

1 SELECTIVE NONCATALYTIC REDUCTION 

FOR NOX

0 0

1 WET SCRUBBER 0 0

1 BAGHOUSE 0 0

Run Name Value UOM Comments

1 Scrubbing Liquid - Total Suspended Solids 1E+05 mg/L

1 Scrubbing Liquid - Total Dissolved Solids 77630 mg/L

2 Scrubbing Liquid - Total Suspended Solids 1E+05 mg/L

2 Scrubbing Liquid - Total Dissolved Solids 77070 mg/L

3 Scrubbing Liquid - Total Suspended Solids 1E+05 mg/L

3 Scrubbing Liquid - Total Dissolved Solids 79720 mg/L

Wednesday, January 12, 2011 Page 19 of 27
Utility Boiler MACT ICR - Clover Power Station Unit 2

Sampling / Stack Data Results Detail

Location Stack Exit - Method 0011

Average

Run Number 3 4 5

Test Date 3/30/2010 3/31/2010 4/2/2010

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 0.217 0.218

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9927 0.9927 0.9927 0.993

Barometric Pressure, inches of Mercury 29.2 29.35 29.55 29.367

Average Orifice Meter Differential, inches H2O 2.16 2.11 1.00 1.757

Dry Gas Meter Volume Sampled, cubic feet 94.713 95.534 87.760 92.669

Average Dry Gas Meter Temperature, °F 74.23 80.94 74.15 76.440

Dry Gas Meter Volume Sampled, dscf 91.182 91.284 85.263 89.243

Total Moisture Liquid collected, g 291.1 289 273.9 284.667

Volume of Water Vapor, standard cubic feet 13.70 13.60 12.89 13.397

Moisture Content of Stack Gas, % 13.06 12.97 13.13 13.053

Moisture Saturation at Stack Gas Temperature, % 12.95 12.56 12.73 12.747

Dry Mole Fraction 0.8705 0.8744 0.8727 0.873

Carbon Dioxide, % 13.21 13.211 13.266 13.229

Oxygen, % 5.912 5.941 5.914 5.922

Carbon Monoxide & Nitrogen, % 80.878 80.848 80.82 80.849

Fuel Factor 1.13 1.13 1.13

Dry Molecular Weight, lb/lb-Mole 30.35 30.35 30.36 30.353

Wet Molecular weight, lb/lb-Mole 28.77 28.87 28.86 28.833

Flue Gas Static Pressure, inches of H2O -1.3 -1.2 -0.95 -1.150

Absolute Flue Gas Pressure, inches of Mercury 29.10 29.26 29.48 29.280

Average Stack Gas Temperature, °F 123.29 122.38 123.13 122.933

Average Velocity Head, inches of H2O 1.1694439071

062

1.160274143

29145

1.007459338

69987

1.112

Average Stack Gas Velocity, feet/second 64.82 64.23 59.67 62.907

Stack Cross-Sectional Area, square feet 388.821 388.821 388.821 388.821

Dry Volumetric Flow Rate, dry scfm 1,158,936.3 1,161,687.3 1,083,818.1 1,134,813.9

00

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,512,202.6 1,498,438.4 1,392,056.9 1,467,565.9

67

Percent Isokinetic of Sampling Rate, % 98.4 98.2 99.2 98.600

Percent Excess Air, % 38.3 38.6 38.3 38.400

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

Round Duct Diameter, inches 267 267 267

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

Wednesday, January 12, 2011 Page 20 of 27
Utility Boiler MACT ICR - Clover Power Station Unit 2

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

Wednesday, January 12, 2011 Page 21 of 27
Utility Boiler MACT ICR - Clover Power Station Unit 2

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

Wednesday, January 12, 2011 Page 22 of 27
Utility Boiler MACT ICR - Clover Power Station Unit 2

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

Wednesday, January 12, 2011 Page 23 of 27
Utility Boiler MACT ICR - Clover Power Station Unit 2

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

Wednesday, January 12, 2011 Page 24 of 27
Utility Boiler MACT ICR - Clover Power Station Unit 2

Location Stack Exit - Method 5/OTM-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

Wednesday, January 12, 2011 Page 25 of 27
Utility Boiler MACT ICR - Clover Power Station Unit 2

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

Wednesday, January 12, 2011 Page 26 of 27
Utility Boiler MACT ICR - Clover Power Station Unit 2

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

Wednesday, January 12, 2011 Page 27 of 27