Name: C.D. Holley

Title: Manager F&H System Operations

Company: Dominion Generation

Sign Date: 8/19/2010

Name: Michael P. Martin

Title: Senior Project Manager

Company: TRC Companies, Inc.

Sign Date: 7/29/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Utility Boiler MACT ICR - Clover Power Station 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.

Wednesday, January 12, 2011 Page 1 of 24
Utility Boiler MACT ICR - Clover Power Station Unit 1

8/19/2010

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:

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:

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 3 180 0

Total organic compounds 

(TOC) as Propane

Method 25A 3 180 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

Stack Exit Selenium Method 29 3 240 0

Wednesday, January 12, 2011 Page 2 of 24
Utility Boiler MACT ICR - Clover Power Station Unit 1

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.

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 Chromium Method 29 3 240 0

Stack Exit Lead Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Cobalt 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 3 180 0

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

Wednesday, January 12, 2011 Page 3 of 24
Utility Boiler MACT ICR - Clover Power Station Unit 1

8/19/2010

Sampling / Stack Data Results Summary

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

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

Wednesday, January 12, 2011 Page 4 of 24
Utility Boiler MACT ICR - Clover Power Station Unit 1

8/19/2010

Location Stack Exit - Method 26A

Average

Run Number 1 2 3

Test Date 4/2/2010 4/3/2010 4/3/2010

Run Start Time

Run Finish Time

Net Run Time, minutes 192 192 192

Dry Gas Meter Volume Sampled, dscf 138.612 138.430 139.786 138.943

Moisture Content of Stack Gas, % 16.09 15.62 15.52 15.743

Moisture Saturation at Stack Gas Temperature, % 13.72 13.64 12.73 13.363

Carbon Dioxide, % 13.01 12.974 12.837 12.940

Oxygen, % 6.161 6.249 6.383 6.264

Average Stack Gas Temperature, °F 125.90 125.67 123.13 124.900

Dry Volumetric Flow Rate, dry scfm 1,084,528.9 1,097,036.1 1,119,055.4 1,100,206.80

0

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,414,686.3 1,430,083.6 1,437,315.7 1,427,361.86

7

Percent Isokinetic of Sampling Rate, % 101.7 100.4 99.4 100.500

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 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

Wednesday, January 12, 2011 Page 5 of 24
Utility Boiler MACT ICR - Clover Power Station Unit 1

8/19/2010

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

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

Wednesday, January 12, 2011 Page 6 of 24
Utility Boiler MACT ICR - Clover Power Station Unit 1

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

Wednesday, January 12, 2011 Page 7 of 24
Utility Boiler MACT ICR - Clover Power Station Unit 1

8/19/2010

Emissions Summary

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 1.73E-02 3.63E-03 2.96E-03 0.008

ppm 1.72E+01 3.58E+00 2.90E+00 7.893

ppm@7%O2 1.62E+01 3.40E+00 2.78E+00 7.460

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000

ppm 0.00E+00 0.00E+00 0.00E+00 0.000

ppm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 1.61 1.52 1.92 1.683

lb/mmBtuO2 3.55E-04 3.38E-04 4.26E-04 0.000

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.763 0.767 0.792 0.774

lb/mmBtuO2 1.68E-04 1.70E-04 1.76E-04 0.000

Location: Stack Exit - Method 29 

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.000843 0.000587 0.000339 0.001

lb/mmBtuO2 1.55E-07 1.04E-07 6.09E-08 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.00194 0.00157 0.00117 0.002

lb/mmBtuO2 3.56E-07 2.77E-07 2.10E-07 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.0002 0.0002 0.0002 0.000

lb/mmBtuO2 3.67E-08 3.53E-08 3.59E-08 0.000

Wednesday, January 12, 2011 Page 8 of 24
Utility Boiler MACT ICR - Clover Power Station Unit 1

8/19/2010

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.00272 0.000352 0.000356 0.001

lb/mmBtuO2 4.99E-07 6.22E-08 6.39E-08 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.0441 0.0556 0.0393 0.046

lb/mmBtuO2 8.09E-06 9.82E-06 7.06E-06 0.000

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.00124 0.00112 0.000792 0.001

lb/mmBtuO2 2.27E-07 1.98E-07 1.42E-07 0.000

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.00271 0.00171 0.00164 0.002

lb/mmBtuO2 4.97E-07 3.02E-07 2.95E-07 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.0596 0.0634 0.0619 0.062

lb/mmBtuO2 1.09E-05 1.12E-05 1.11E-05 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.0591 0.0527 0.0366 0.049

lb/mmBtuO2 1.08E-05 9.31E-06 6.57E-06 0.000

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.023 0.0184 0.0194 0.020

lb/mmBtuO2 4.22E-06 3.25E-06 3.48E-06 0.000

Location: Stack Exit - Method 5/OTM-28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 20.5 15.3 14.5 16.767

lb/mmBtuO2 3.75E-03 2.60E-03 2.55E-03 0.003

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 7.9 483.7 27.4 173.000

Wednesday, January 12, 2011 Page 9 of 24
Utility Boiler MACT ICR - Clover Power Station Unit 1

8/19/2010

Process Run Data

lb/mmBtuO2 1.45E-03 8.21E-02 4.82E-03 0.029

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 1.6 41 2.1 14.900

lb/mmBtuO2 2.93E-04 6.96E-03 3.69E-04 0.003

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 28 538 42 202.667

lb/mmBtuO2 5.13E-03 9.14E-02 7.39E-03 0.035

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

lb/mmBtuO2 4.63E-02 4.26E-02 4.26E-02 0.044

ppm 2.01E+01 1.84E+01 1.82E+01 18.900

ppm@7%O2 1.90E+01 1.75E+01 1.74E+01 17.967

Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

lb/mmBtuO2 2.84E-01 3.18E-01 3.33E-01 0.312

ppm 1.71E+02 1.91E+02 1.98E+02 186.667

ppm@7%O2 1.61E+02 1.81E+02 1.90E+02 177.333

Wednesday, January 12, 2011 Page 10 of 24
Utility Boiler MACT ICR - Clover Power Station Unit 1

8/19/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input 4244.1 Million Btus/hr Collected during 

M29 run 1

Collected during 

M29 run 1 and 

M5/OTM28 run 1

0

1 Steam Output 3285.5 1000 lb steam/hr Collected during 

M29 run 1 and

M5/OTM28 run 1

0

1 Fuel Oil Firing Rate 0 gal/hr Collected during 

M29 run 1 and

M5/OTM28 run 1

0

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

M29 run 1 and

M5/OTM28 run 1

0

1 Pressure Drop Across FGD 2.4 in H20 Collected during 

M29 run 1 and

M5/OTM28 run 1

0

1 Flue Gas Carbon Dioxide Content 12.31 % Collected during 

M29 run 1 and

M5/OTM28 run 1

0

1 Flue Gas Sampling Point Temperature 127.6 Deg F Collected during 

M29 run 1 and

M5/OTM28 run 1

0

1 Unit Gross Electrical Output 460.5 Mwe Collected during 

M29 run 1 and

M5/OTM28 run 1

0

1 Unit Net Electric Generation 430.92 MWh Collected during 

M29 run 1 and

M5/OTM28 run 1

0

2 Heat Input 4169.5 Million Btus/hr Collected during 

M29 run 2 and

M5/OTM28 run 2

0

2 Steam Output 3266.6 1000 lb steam/hr Collected during 

M29 run 2 and

M5/OTM28 run 2

0

2 Fuel Oil Firing Rate 0 gal/hr Collected during 

M29 run 2 and

M5/OTM28 run 2

0

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

M29 run 2 and

M5/OTM28 run 2

0

2 Pressure Drop Across FGD 2.37 in H20 Collected during 

M29 run 2 and

M5/OTM28 run 2

0

Wednesday, January 12, 2011 Page 11 of 24
Utility Boiler MACT ICR - Clover Power Station Unit 1

8/19/2010

2 Flue Gas Carbon Dioxide Content 12 % Collected during 

M29 run 2 and

M5/OTM28 run 2

0

2 Flue Gas Sampling Point Temperature 126.4 Deg F Collected during 

M29 run 2 and

M5/OTM28 run 2

0

2 Unit Gross Electrical Output 459.17 Mwe Collected during 

M29 run 2 and

M5/OTM28 run 2

0

2 Unit Net Electric Generation 429.52 MWh Collected during 

M29 run 2 and

M5/OTM28 run 2

0

3 Heat Input 4232.7 Million Btus/hr Collected during 

M29 run 3 and

M5/OTM28 run 3

0

3 Steam Output 3256.1 1000 lb steam/hr Collected during 

M29 run 3 and

M5/OTM28 run 3

0

3 Fuel Oil Firing Rate 0 gal/hr Collected during 

M29 run 3 and

M5/OTM28 run 3

0

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

M29 run 3 and

M5/OTM28 run 3

0

3 Pressure Drop Across FGD 2.68 in H20 Collected during 

M29 run 3 and

M5/OTM28 run 3

0

3 Flue Gas Carbon Dioxide Content 11.63 % Collected during 

M29 run 3 and

M5/OTM28 run 3

0

3 Flue Gas Sampling Point Temperature 126.63 Deg F Collected during 

M29 run 3 and

M5/OTM28 run 3

0

3 Unit Gross Electrical Output 458.4 Mwe Collected during 

M29 run 3 and

M5/OTM28 run 3

0

3 Unit Net Electric Generation 427.52 MWh Collected during 

M29 run 3 and

M5/OTM28 run 3

0

4 Heat Input 4119.9 Million Btus/hr Collected during 

M26A run 1

0

4 Steam Output 3136.5 1000 lb steam/hr Collected during 

M26A run 1

0

4 Fuel Oil Firing Rate 0 gal/hr Collected during 

M26A run 1

0

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

M26A run 1

0

Wednesday, January 12, 2011 Page 12 of 24
Utility Boiler MACT ICR - Clover Power Station Unit 1

8/19/2010

4 Pressure Drop Across FGD 2.47 in H20 Collected during 

M26A run 1

0

4 Flue Gas Carbon Dioxide Content 11.41 % Collected during 

M26A run 1

0

4 Flue Gas Sampling Point Temperature 128.55 Deg F Collected during 

M26A run 1

0

4 Unit Gross Electrical Output 436.5 Mwe Collected during 

M26A run 1

0

4 Unit Net Electric Generation 407.57 MWh Collected during 

M26A run 1

0

5 Heat Input 4091.6 Million Btus/hr Collected during 

M26A run 2

0

5 Steam Output 3095.7 1000 lb steam/hr Collected during 

M26A run 2

0

5 Fuel Oil Firing Rate 0 gal/hr Collected during 

M26A run 2

0

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

M26A run 2

0

5 Pressure Drop Across FGD 2.4 in H20 Collected during 

M26A run 2

0

5 Flue Gas Carbon Dioxide Content 11.45 % Collected during 

M26A run 2

0

5 Flue Gas Sampling Point Temperature 127.25 Deg F Collected during 

M26A run 2

0

5 Unit Gross Electrical Output 437 Mwe Collected during 

M26A run 2

0

5 Unit Net Electric Generation 407.21 MWh Collected during 

M26A run 2

0

6 Heat Input 4108.6 Million Btus/hr Collected during 

M26A run 3

0

6 Steam Output 3114.8 1000 lb steam/hr Collected during 

M26A run 3

0

6 Fuel Oil Firing Rate 0 gal/hr Collected during 

M26A run 3

0

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

M26A run 3

0

6 Pressure Drop Across FGD 2.4 in H20 Collected during 

M26A run 3

0

6 Flue Gas Carbon Dioxide Content 11.41 % Collected during 

M26A run 3

0

6 Flue Gas Sampling Point Temperature 127.31 Deg F Collected during 

M26A run 3

0

6 Unit Gross Electrical Output 436.75 Mwe Collected during 

M26A run 3

0

6 Unit Net Electric Generation 407.82 MWh Collected during 

M26A run 3

0

Wednesday, January 12, 2011 Page 13 of 24
Utility Boiler MACT ICR - Clover Power Station Unit 1

8/19/2010

7 Heat Input 4123.4 Million Btus/hr Collected during 

run 1 of Method 

10, 6C, 7E, 25A

0

7 Steam Output 3124.6 1000 lb steam/hr Collected during 

run 1 of Method 

10, 6C, 7E, 25A

0

7 Fuel Oil Firing Rate 0 gal/hr Collected during 

run 1 of Method 

10, 6C, 7E, 25A

0

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

run 1 of Method 

10, 6C, 7E, 25A

0

7 Pressure Drop Across FGD 2.46 in H20 Collected during 

run 1 of Method 

10, 6C, 7E, 25A

0

7 Flue Gas Carbon Dioxide Content 11.55 % Collected during 

run 1 of Method 

10, 6C, 7E, 25A

0

7 Flue Gas Sampling Point Temperature 128.93 Deg F Collected during 

run 1 of Method 

10, 6C, 7E, 25A

0

7 Unit Gross Electrical Output 436 Mwe Collected during 

run 1 of Method 

10, 6C, 7E, 25A

0

7 Unit Net Electric Generation 405.94 MWh Collected during 

run 1 of Method 

10, 6C, 7E, 25A

0

8 Heat Input 4088.1 Million Btus/hr Collected during 

run 2 of Method 

10, 6C, 7E, 25A

0

8 Steam Output 3101.7 1000 lb steam/hr Collected during 

run 2 of Method 

10, 6C, 7E, 25A

0

8 Fuel Oil Firing Rate 0 gal/hr Collected during 

run 2 of Method 

10, 6C, 7E, 25A

0

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

run 2 of Method 

10, 6C, 7E, 25A

0

8 Pressure Drop Across FGD 2.4 in H20 Collected during 

run 2 of Method 

10, 6C, 7E, 25A

0

8 Flue Gas Carbon Dioxide Content 11.48 % Collected during 

run 2 of Method 

10, 6C, 7E, 25A

0

8 Flue Gas Sampling Point Temperature 127.31 Deg F Collected during 

run 2 of Method 

10, 6C, 7E, 25A

0

Wednesday, January 12, 2011 Page 14 of 24
Utility Boiler MACT ICR - Clover Power Station Unit 1

8/19/2010

8 Unit Gross Electrical Output 437 Mwe Collected during 

run 2 of Method 

10, 6C, 7E, 25A

0

8 Unit Net Electric Generation 407.75 MWh Collected during 

run 2 of Method 

10, 6C, 7E, 25A

0

9 Heat Input 4131.1 Million Btus/hr Collected during 

run 3 of Method 

10, 6C, 7E, 25A

0

9 Steam Output 3122.2 1000 lb steam/hr Collected during 

run 3 of Method 

10, 6C, 7E, 25A

0

9 Fuel Oil Firing Rate 0 gal/hr Collected during 

run 3 of Method 

10, 6C, 7E, 25A

0

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

run 3 of Method 

10, 6C, 7E, 25A

0

9 Pressure Drop Across FGD 2.4884 in H20 Collected during 

run 3 of Method 

10, 6C, 7E, 25A

0

9 Flue Gas Carbon Dioxide Content 11.39 % Collected during 

run 3 of Method 

10, 6C, 7E, 25A

0

9 Flue Gas Sampling Point Temperature 127.53 Deg F Collected during 

run 3 of Method 

10, 6C, 7E, 25A

0

9 Unit Gross Electrical Output 436.67 Mwe Collected during 

run 3 of Method 

10, 6C, 7E, 25A

0

9 Unit Net Electric Generation 407.71 MWh Collected during 

run 3 of Method 

10, 6C, 7E, 25A

0

1 Coal Firing Rate 172.62 tons/day Collected during 

M29 run 1

Collected during 

M29 run 1 and 

M5/OTM28 run 1

0

1 FGD Scrubber Liquor Flow Rate 150727 gal/min Collected during 

M29 run 1

Collected during 

M29 run 1 and 

M5/OTM28 run 1

0

2 Coal Firing Rate 172.81 tons/day Collected during 

M29 run 2 and

M5/OTM28 run 2

0

2 FGD Scrubber Liquor Flow Rate 150727 gal/min Collected during 

M29 run 2 and

M5/OTM28 run 2

0

Wednesday, January 12, 2011 Page 15 of 24
Utility Boiler MACT ICR - Clover Power Station Unit 1

8/19/2010

APCD Run Data

3 Coal Firing Rate 178.87 tons/day Collected during 

M29 run 3 and

M5/OTM28 run 3

0

3 FGD Scrubber Liquor Flow Rate 150727 gal/min Collected during 

M29 run 3 and

M5/OTM28 run 3

0

4 Coal Firing Rate 163.03 tons/day Collected during 

M26A run 1

0

4 FGD Scrubber Liquor Flow Rate 150727 gal/min Collected during 

M26A run 1

0

5 Coal Firing Rate 161.92 tons/day Collected during 

M26A run 2

0

5 FGD Scrubber Liquor Flow Rate 150727 gal/min Collected during 

M26A run 2

0

6 Coal Firing Rate 161.64 tons/day Collected during 

M26A run 3

0

6 FGD Scrubber Liquor Flow Rate 150727 gal/min Collected during 

M26A run 3

0

7 Coal Firing Rate 162.71 tons/day Collected during 

run 1 of Method 

10, 6C, 7E, 25A

0

7 FGD Scrubber Liquor Flow Rate 150727 gal/min Collected during 

run 1 of Method 

10, 6C, 7E, 25A

0

8 Coal Firing Rate 161.52 tons/day Collected during 

run 2 of Method 

10, 6C, 7E, 25A

0

8 FGD Scrubber Liquor Flow Rate 150727 gal/min Collected during 

run 2 of Method 

10, 6C, 7E, 25A

0

9 Coal Firing Rate 162.11 tons/day Collected during 

run 3 of Method 

10, 6C, 7E, 25A

0

9 FGD Scrubber Liquor Flow Rate 150727 gal/min Collected during 

run 3 of Method 

10, 6C, 7E, 25A

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

Wednesday, January 12, 2011 Page 16 of 24
Utility Boiler MACT ICR - Clover Power Station Unit 1

8/19/2010

Process Lab Run Data

Run Name Value UOM Comments

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

1 Scrubbing Liquid - Total Dissolved Solids 90280 mg/L

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

2 Scrubbing Liquid - Total Dissolved Solids 86840 mg/L

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

3 Scrubbing Liquid - Total Dissolved Solids 83310 mg/L

Wednesday, January 12, 2011 Page 17 of 24
Utility Boiler MACT ICR - Clover Power Station Unit 1

8/19/2010

Sampling / Stack Data Results Detail

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 18 of 24
Utility Boiler MACT ICR - Clover Power Station Unit 1

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

Wednesday, January 12, 2011 Page 19 of 24
Utility Boiler MACT ICR - Clover Power Station Unit 1

8/19/2010

Location Stack Exit - Method 26A

Average

Run Number 1 2 3

Test Date 4/2/2010 4/3/2010 4/3/2010

Run Start Time

Run Finish Time

Net Traversing Points 48 48 48

Net Run Time, minutes 192 192 192

Nozzle Diameter, inches 0.216 0.216 0.216 0.216

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9916 0.9916 0.9916 0.992

Barometric Pressure, inches of Mercury 29.55 29.55 29.55 29.550

Average Orifice Meter Differential, inches H2O 1.87 1.85 1.99 1.903

Dry Gas Meter Volume Sampled, cubic feet 147.765 144.956 147.014 146.578

Average Dry Gas Meter Temperature, °F 93.80 83.96 86.52 88.093

Dry Gas Meter Volume Sampled, dscf 138.612 138.430 139.786 138.943

Total Moisture Liquid collected, g 564.7 544.5 545.7 551.633

Volume of Water Vapor, standard cubic feet 26.58 25.63 25.69 25.967

Moisture Content of Stack Gas, % 16.09 15.62 15.52 15.743

Moisture Saturation at Stack Gas Temperature, % 13.72 13.64 12.73 13.363

Dry Mole Fraction 0.8628 0.8636 0.8727 0.866

Carbon Dioxide, % 13.01 12.974 12.837 12.940

Oxygen, % 6.161 6.249 6.383 6.264

Carbon Monoxide & Nitrogen, % 80.829 80.777 80.78 80.795

Fuel Factor 1.13 1.13 1.13

Dry Molecular Weight, lb/lb-Mole 30.33 30.33 30.31 30.323

Wet Molecular weight, lb/lb-Mole 29.06 29.00 29.25 29.103

Flue Gas Static Pressure, inches of H2O -0.73 -1 -1 -0.910

Absolute Flue Gas Pressure, inches of Mercury 29.50 29.48 29.48 29.487

Average Stack Gas Temperature, °F 125.90 125.67 123.13 124.900

Average Velocity Head, inches of H2O 1.0432460117

5448

1.063574948

01302

1.088418093

92919

1.065

Average Stack Gas Velocity, feet/second 60.64 61.30 61.61 61.183

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

Dry Volumetric Flow Rate, dry scfm 1,084,528.9 1,097,036.1 1,119,055.4 1,100,206.8

00

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,414,686.3 1,430,083.6 1,437,315.7 1,427,361.8

67

Percent Isokinetic of Sampling Rate, % 101.7 100.4 99.4 100.500

Percent Excess Air, % 40.6 41.4 42.7 41.567

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 24
Utility Boiler MACT ICR - Clover Power Station Unit 1

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

Wednesday, January 12, 2011 Page 21 of 24
Utility Boiler MACT ICR - Clover Power Station Unit 1

8/19/2010

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 22 of 24
Utility Boiler MACT ICR - Clover Power Station Unit 1

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

Wednesday, January 12, 2011 Page 23 of 24
Utility Boiler MACT ICR - Clover Power Station Unit 1

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

Wednesday, January 12, 2011 Page 24 of 24