Name: Steve Strunk

Title: Specialist Air Permitting Compliance

Company: Tennessee Valley Authority

Sign Date: 9/30/2010

Name: Jim Diederich

Title: System Engineer Perf. Evaluation

Company: Tennessee Valley Authority

Sign Date: 9/30/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Final Test Report 

for

/ /

Based on information and belief formed 

after reasonable inquiry, I certify that the 

statements and information in this test 

report are true, accurate, and complete.

I have reviewed all testing details and 

results in this test report and hereby 

certify that the test report is authentic 

and accurate.

Tuesday, February 15, 2011 Page 1 of 22
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Facility Information:

Cumberland Fossil Plant Unit 1

815 Cumberland City Road

Cumberland City TN 37050

Contact: Steve Strunk

Phone: 423-751-2808

Fax: 423-751-7011

Email: scstrunk@tva.gov

Testing Company:

TVA Performance Engineering

1101 Market Street

PSC 1B-C

Chattanooga TN 37402

Contact:Jim Diederich

Phone: 423-876-6730

Fax: 423-876-6734

Email: jadiederich@tva.gov

Air Permit Number:

546465

Permitted Source ID/Name:

3399 Cumberland Fossil Plant

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

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

 process flow diagram:

Cumberland Unit 1 is a pulverized coal-fired, supercritical, cell-fired once-through steam generator with a Maximum 

Continuous Rating of 10 Mlb/hr reheat steam flow. Steam pressure at the turbine first stage is 3500 psig. Final 

superheat and reheat temperatures are 1003°F. There are 88 burners installed in an opposed firing pattern four rows 

high on both the front and rear wall. 11 MPS 89 mills feed pulverized coal to the burners. The unit is equipped with 

low NOx burners and a selective catalyst reduction (SCR) system for NOx emissions control, an electrostatic 

precipitator for removal of particulate matter as well as a wet scrubber for control of SO2 emissions and additional 

particulate removal.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 4716100011 FRS #: 110000493127

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 462 0 0 0 1617 3095.4 4 16

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack 2,3,7,8-TCDD Method 23 3 600 0

Stack 1,2,3,7,8-PeCDD Method 23 3 600 0

Stack 1,2,3,4,7,8-HxCDD Method 23 3 600 0

Stack 1,2,3,6,7,8-HxCDD Method 23 3 600 0

Tuesday, February 15, 2011 Page 2 of 22
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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.

MANUAL COAL COLLECTION IN SUPPORT OF HAPS TESTING AT CUF

Preliminary communication with plant operations and engineering indicated that manual sampling from the coal 

feeders prior to the pulverizers would be possible because it is regularly performed to collect “grab” samples. On 

June 8, prior to the beginning of HAPS sampling, in conversations with operations we determined that due to the 

positive pressure in the feed system that a gate would need to be closed between the pulverizer and the feeder while 

samples were being collected. This was not an issue until we discovered that oil guns automatically came on to 

Stack 1,2,3,7,8,9-HxCDD Method 23 3 600 0

Stack 1,2,3,4,6,7,8-HpCDD Method 23 3 600 0

Stack OCDD Method 23 3 600 0

Stack 2,3,7,8-TCDF Method 23 3 600 0

Stack 1,2,3,7,8-PeCDF Method 23 3 600 0

Stack 2,3,4,7,8-PeCDF Method 23 3 600 0

Stack 1,2,3,4,7,8-HxCDF Method 23 3 600 0

Stack 1,2,3,6,7,8-HxCDF Method 23 3 600 0

Stack 2,3,4,6,7,8-HxCDF Method 23 3 600 0

Stack 1,2,3,7,8,9-HxCDF Method 23 3 600 0

Stack 1,2,3,4,6,7,8-HpCDF Method 23 3 600 0

Stack 1,2,3,4,7,8,9-HpCDF Method 23 3 600 0

Stack OCDF Method 23 3 600 0

Stack Other TCDD Method 23 3 600 0

Stack Other PeCDD Method 23 3 600 0

Stack Other HxCDD Method 23 3 600 0

Stack Other HpCDD Method 23 3 600 0

Stack Other TCDF Method 23 3 600 0

Stack Other PeCDF Method 23 3 600 0

Stack Other HxCDF Method 23 3 600 0

Stack Other HpCDF Method 23 3 600 0

Stack Total Dioxins Method 23 3 600 0

Stack Total Furans Method 23 3 600 0

Stack 3,3',4,4'-TCB (PCB77) Method 23 3 600 0

Stack 3,4,4',5-TCB (PCB81) Method 23 3 600 0

Stack 2,3,3',4,4'-PeCB (PCB105) Method 23 3 600 0

Stack 2,3,4,4',5-PeCB (PCB114) Method 23 3 600 0

Stack 2,3',4,4',5-PeCB (PCB118) Method 23 3 600 0

Stack 2',3,4,4',5-PeCB (PCB123) Method 23 3 600 0

Stack 3,3',4,4',5-PeCB (PCB126) Method 23 3 600 0

2,3,3',4,4',5/2,3,3',4,4',5'-

HxCB (PCBs156/157)

Stack Method 23 3 600 0

Stack 2,3',4,4',5,5'-HxCB (PCB167) Method 23 3 600 0

Stack 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 600 0

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

(PCB189)

Stack Method 23 3 600 0

Stack Hydrogen Chloride Method 26A 3 180 0

Stack Hydrogen Fluoride Method 26A 3 180 0

Stack Co2 Method 3A CO2 3 180 0

Stack O2 Method 3A O2 3 180 0

Stack Sulfur Dioxide Method 6C 3 180 0

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

Tuesday, February 15, 2011 Page 3 of 22
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maintain a flame when a pulverizer was isolated. It was calculated that the oil input would constitute 3% to 5% of the 

Btus for the test period. The input of the oil firing was considered to be too significant to collect samples from the 

feeders. 

Another possible sample collection point considered was the pipe between the coal bunker and the belt feeder. 

However, there was no way to collect a sample that would comply with ASTM coal sampling standards. 

The decision was made to collect the manual coal samples from the head pulleys of the belts feeding the bunkers. 

All samples were collected using methods that comply with ASTM standards. The bunker feed belts do not run 

continuously as the feeders, so the coal was collected during the bunker filling run during or prior to the stack test.

Tuesday, February 15, 2011 Page 4 of 22
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Tuesday, February 15, 2011 Page 5 of 22
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Sampling / Stack Data Results Summary

Location Stack - Method 23

Average

Run Number 1 2 3

Test Date 6/10/2010 6/17/2010 6/18/2010

Run Start Time 10:30:00 AM 8:41:00 

AM

8:42:00 AM

Run Finish Time 9:16:00 PM 6:43:00 PM 6:44:00 PM

Net Run Time, minutes 576 576 576

Dry Gas Meter Volume Sampled, dscf 313.485 322.201 320.581 318.756

Moisture Content of Stack Gas, % 16.68 16.43 17.19 16.767

Moisture Saturation at Stack Gas Temperature, % 15.53 15.06 15.40 15.330

Carbon Dioxide, % 11.95 11.67 11.84 11.820

Oxygen, % 7.39 7.43 7.47 7.430

Average Stack Gas Temperature, °F 129.92 128.88 129.69 129.497

Dry Volumetric Flow Rate, dry scfm 3,318,677.7 3,433,506.6 3,436,897.3 3,396,360.53

3

Actual Wet Volumetric Flue Gas Flow Rate, acfm 4,524,143.0 4,633,806.5 4,666,635.7 4,608,195.06

7

Percent Isokinetic of Sampling Rate, % 97.5 98.6 98.0 98.033

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

Tuesday, February 15, 2011 Page 6 of 22
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Location Stack - 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

Location Stack - Method 3A CO2

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

Tuesday, February 15, 2011 Page 7 of 22
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Location Stack - Method 3A O2

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 - 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

Tuesday, February 15, 2011 Page 8 of 22
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Location Stack - 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

Tuesday, February 15, 2011 Page 9 of 22
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Emissions Summary

Location: Stack - Method 23

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000086 0.000000008 0.0000000072 0.000

lb/mmBtuO2 9.15E-13 8.31E-13 7.54E-13 0.000

ng/dscm 9.69E-04 8.77E-04 7.93E-04 0.001

ng/dscm@7%O2 9.97E-04 9.05E-04 8.21E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000042 0.0000000053 0.0000000036 0.000

lb/mmBtuO2 4.47E-13 5.50E-13 3.77E-13 0.000

ng/dscm 4.73E-04 5.81E-04 3.97E-04 0.000

ng/dscm@7%O2 4.87E-04 6.00E-04 4.11E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000054 0.0000000069 0.0000000048 0.000

lb/mmBtuO2 5.75E-13 7.16E-13 5.02E-13 0.000

ng/dscm 6.08E-04 7.56E-04 5.29E-04 0.001

ng/dscm@7%O2 6.26E-04 7.80E-04 5.48E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000053 0.000000005 0.0000000046 0.000

lb/mmBtuO2 5.64E-13 5.19E-13 4.81E-13 0.000

ng/dscm 5.97E-04 5.48E-04 5.07E-04 0.001

ng/dscm@7%O2 6.14E-04 5.65E-04 5.25E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000033 0.0000000032 0.0000000031 0.000

lb/mmBtuO2 3.51E-13 3.32E-13 3.24E-13 0.000

ng/dscm 3.72E-04 3.51E-04 3.42E-04 0.000

ng/dscm@7%O2 3.83E-04 3.62E-04 3.54E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000051 0.0000000049 0.0000000045 0.000

lb/mmBtuO2 5.43E-13 5.09E-13 4.71E-13 0.000

ng/dscm 5.75E-04 5.37E-04 4.96E-04 0.001

ng/dscm@7%O2 5.92E-04 5.54E-04 5.13E-04 0.001

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

Average

Tuesday, February 15, 2011 Page 10 of 22
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RunNumber 1 2 3

Mass_mg 0.0000000031 0.0000000029 0.0000000028 0.000

lb/mmBtuO2 3.30E-13 3.01E-13 2.93E-13 0.000

ng/dscm 3.49E-04 3.18E-04 3.08E-04 0.000

ng/dscm@7%O2 3.59E-04 3.28E-04 3.19E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000052 0.000000005 0.0000000046 0.000

lb/mmBtuO2 5.53E-13 5.19E-13 4.81E-13 0.000

ng/dscm 5.86E-04 5.48E-04 5.07E-04 0.001

ng/dscm@7%O2 6.03E-04 5.65E-04 5.25E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000037 0.0000000035 0.0000000034 0.000

lb/mmBtuO2 3.94E-13 3.63E-13 3.56E-13 0.000

ng/dscm 4.17E-04 3.84E-04 3.75E-04 0.000

ng/dscm@7%O2 4.29E-04 3.96E-04 3.88E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000059 0.0000000063 0.000000007 0.000

lb/mmBtuO2 6.28E-13 6.54E-13 7.33E-13 0.000

ng/dscm 6.65E-04 6.91E-04 7.71E-04 0.001

ng/dscm@7%O2 6.84E-04 7.13E-04 7.98E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000051 0.000000005 0.0000000058 0.000

lb/mmBtuO2 5.43E-13 5.19E-13 6.07E-13 0.000

ng/dscm 5.75E-04 5.48E-04 6.39E-04 0.001

ng/dscm@7%O2 5.92E-04 5.65E-04 6.61E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000113 0.0000000128 0.0000000119 0.000

lb/mmBtuO2 1.20E-12 1.33E-12 1.25E-12 0.000

ng/dscm 1.27E-03 1.40E-03 1.31E-03 0.001

ng/dscm@7%O2 1.31E-03 1.44E-03 1.36E-03 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000795 0.0000000455 0.0000000326 0.000

lb/mmBtuO2 8.46E-12 4.72E-12 3.41E-12 0.000

ng/dscm 8.96E-03 4.99E-03 3.59E-03 0.006

ng/dscm@7%O2 9.22E-03 5.15E-03 3.72E-03 0.006

Tuesday, February 15, 2011 Page 11 of 22
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Compound: 2,3,3',4,4'-PeCB (PCB105)

Average

RunNumber 1 2 3

Mass_mg 0.0000003458 0.0000001775 0.0000001523 0.000

lb/mmBtuO2 3.68E-11 1.84E-11 1.59E-11 0.000

ng/dscm 3.90E-02 1.95E-02 1.68E-02 0.025

ng/dscm@7%O2 4.01E-02 2.01E-02 1.74E-02 0.026

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000122 0.0000000179 0.000000011 0.000

lb/mmBtuO2 1.30E-12 1.86E-12 1.15E-12 0.000

ng/dscm 1.37E-03 1.96E-03 1.21E-03 0.002

ng/dscm@7%O2 1.41E-03 2.02E-03 1.25E-03 0.002

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000195 0.0000000135 0.0000000126 0.000

lb/mmBtuO2 2.07E-12 1.40E-12 1.32E-12 0.000

ng/dscm 2.20E-03 1.48E-03 1.39E-03 0.002

ng/dscm@7%O2 2.26E-03 1.53E-03 1.44E-03 0.002

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

Average

RunNumber 1 2 3

Mass_mg 0.000000869 0.00000046 0.000000519 0.000

lb/mmBtuO2 9.25E-11 4.78E-11 5.43E-11 0.000

ng/dscm 9.79E-02 5.04E-02 5.72E-02 0.069

ng/dscm@7%O2 1.01E-01 5.20E-02 5.92E-02 0.071

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000137 0.000000015 0.0000000137 0.000

lb/mmBtuO2 1.46E-12 1.56E-12 1.43E-12 0.000

ng/dscm 1.54E-03 1.64E-03 1.51E-03 0.002

ng/dscm@7%O2 1.58E-03 1.69E-03 1.56E-03 0.002

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000032 0.000000003 0.000000003 0.000

lb/mmBtuO2 3.40E-13 3.11E-13 3.14E-13 0.000

ng/dscm 3.61E-04 3.29E-04 3.31E-04 0.000

ng/dscm@7%O2 3.71E-04 3.40E-04 3.43E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000051 0.0000000051 0.0000000058 0.000

lb/mmBtuO2 5.43E-13 5.30E-13 6.07E-13 0.000

Tuesday, February 15, 2011 Page 12 of 22
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ng/dscm 5.75E-04 5.59E-04 6.39E-04 0.001

ng/dscm@7%O2 5.92E-04 5.77E-04 6.61E-04 0.001

Compound: 2,3,7,8-TCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000108 0.0000000118 0.0000000132 0.000

lb/mmBtuO2 1.15E-12 1.23E-12 1.38E-12 0.000

ng/dscm 1.22E-03 1.29E-03 1.45E-03 0.001

ng/dscm@7%O2 1.26E-03 1.33E-03 1.50E-03 0.001

Compound: 2,3,7,8-TCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000119 0.0000000092 0.0000000148 0.000

lb/mmBtuO2 1.27E-12 9.55E-13 1.55E-12 0.000

ng/dscm 1.34E-03 1.01E-03 1.63E-03 0.001

ng/dscm@7%O2 1.38E-03 1.04E-03 1.69E-03 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000128 0.0000000125 0.0000000115 0.000

lb/mmBtuO2 1.36E-12 1.30E-12 1.20E-12 0.000

ng/dscm 1.44E-03 1.37E-03 1.27E-03 0.001

ng/dscm@7%O2 1.48E-03 1.41E-03 1.31E-03 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000135 0.0000000143 0.0000000131 0.000

lb/mmBtuO2 1.44E-12 1.48E-12 1.37E-12 0.000

ng/dscm 1.52E-03 1.57E-03 1.44E-03 0.002

ng/dscm@7%O2 1.56E-03 1.62E-03 1.49E-03 0.002

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000336 0.000000017 0.0000000152 0.000

lb/mmBtuO2 3.58E-12 1.77E-12 1.59E-12 0.000

ng/dscm 3.79E-03 1.86E-03 1.67E-03 0.002

ng/dscm@7%O2 3.90E-03 1.92E-03 1.73E-03 0.003

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

Average

RunNumber 1 2 3

Mass_mg 0.000000017 0.0000000167 0.0000000146 0.000

lb/mmBtuO2 1.81E-12 1.73E-12 1.53E-12 0.000

ng/dscm 1.92E-03 1.83E-03 1.61E-03 0.002

ng/dscm@7%O2 1.98E-03 1.89E-03 1.67E-03 0.002

Compound: OCDD

Average

RunNumber 1 2 3

Tuesday, February 15, 2011 Page 13 of 22
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Mass_mg 0.0000000108 0.0000000096 0.000000006 0.000

lb/mmBtuO2 1.15E-12 9.97E-13 6.28E-13 0.000

ng/dscm 1.22E-03 1.05E-03 6.61E-04 0.001

ng/dscm@7%O2 1.26E-03 1.08E-03 6.84E-04 0.001

Compound: OCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000071 0.0000000085 0.0000000056 0.000

lb/mmBtuO2 7.55E-13 8.83E-13 5.86E-13 0.000

ng/dscm 8.00E-04 9.32E-04 6.17E-04 0.001

ng/dscm@7%O2 8.23E-04 9.62E-04 6.39E-04 0.001

Compound: Other HpCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000086 0.000000008 0.0000000072 0.000

lb/mmBtuO2 9.15E-13 8.31E-13 7.54E-13 0.000

ng/dscm 9.69E-04 8.77E-04 7.93E-04 0.001

ng/dscm@7%O2 9.97E-04 9.05E-04 8.21E-04 0.001

Compound: Other HpCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000048 0.000000006 0.0000000042 0.000

lb/mmBtuO2 5.11E-13 6.23E-13 4.40E-13 0.000

ng/dscm 5.41E-04 6.58E-04 4.63E-04 0.001

ng/dscm@7%O2 5.57E-04 6.79E-04 4.79E-04 0.001

Compound: Other HxCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000165 0.0000000213 0.0000000129 0.000

lb/mmBtuO2 1.76E-12 2.21E-12 1.35E-12 0.000

ng/dscm 1.86E-03 2.33E-03 1.42E-03 0.002

ng/dscm@7%O2 1.91E-03 2.40E-03 1.47E-03 0.002

Compound: Other HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000084 0.0000000134 0.0000000031 0.000

lb/mmBtuO2 8.94E-13 1.39E-12 3.24E-13 0.000

ng/dscm 9.46E-04 1.47E-03 3.42E-04 0.001

ng/dscm@7%O2 9.73E-04 1.52E-03 3.54E-04 0.001

Compound: Other PeCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000059 0.0000000064 0.000000007 0.000

lb/mmBtuO2 6.28E-13 6.65E-13 7.33E-13 0.000

ng/dscm 6.65E-04 7.02E-04 7.71E-04 0.001

ng/dscm@7%O2 6.84E-04 7.24E-04 7.98E-04 0.001

Tuesday, February 15, 2011 Page 14 of 22
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Compound: Other PeCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000131 0.0000000099 0.0000000058 0.000

lb/mmBtuO2 1.39E-12 1.03E-12 6.07E-13 0.000

ng/dscm 1.48E-03 1.09E-03 6.39E-04 0.001

ng/dscm@7%O2 1.52E-03 1.12E-03 6.61E-04 0.001

Compound: Other TCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000111 0.0000000241 0.0000000136 0.000

lb/mmBtuO2 1.18E-12 2.50E-12 1.42E-12 0.000

ng/dscm 1.25E-03 2.64E-03 1.50E-03 0.002

ng/dscm@7%O2 1.29E-03 2.72E-03 1.55E-03 0.002

Compound: Other TCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000109 0.0000000116 0.0000000122 0.000

lb/mmBtuO2 1.16E-12 1.20E-12 1.28E-12 0.000

ng/dscm 1.23E-03 1.27E-03 1.34E-03 0.001

ng/dscm@7%O2 1.27E-03 1.31E-03 1.39E-03 0.001

Compound: Total Dioxins

Average

RunNumber 1 2 3

Mass_mg 0.0000000529 0.0000000694 0.0000000467 0.000

lb/mmBtuO2 5.63E-12 7.21E-12 4.89E-12 0.000

ng/dscm 5.96E-03 7.61E-03 5.15E-03 0.006

ng/dscm@7%O2 6.13E-03 7.85E-03 5.33E-03 0.006

Compound: Total Furans

Average

RunNumber 1 2 3

Mass_mg 0.0000000523 0.0000000552 0.0000000402 0.000

lb/mmBtuO2 5.56E-12 5.73E-12 4.21E-12 0.000

ng/dscm 5.89E-03 6.05E-03 4.43E-03 0.005

ng/dscm@7%O2 6.06E-03 6.24E-03 4.59E-03 0.006

Location: Stack - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 0.92 0.982 1.02 0.974

lb/mmBtuO2 3.19E-04 3.09E-04 3.22E-04 0.000

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.37 0.48 0.48 0.443

lb/mmBtuO2 1.28E-04 1.51E-04 1.51E-04 0.000

Tuesday, February 15, 2011 Page 15 of 22
9/30/2010

Process Run Data

Location: Stack - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

lb/mmBtuO2 1.11E-01 1.47E-01 1.39E-01 0.132

ppm 4.28E+01 5.79E+01 5.52E+01 51.967

ppm@7%O2 4.55E+01 6.02E+01 5.70E+01 54.233

Location: Stack - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

lb/mmBtuO2 3.87E-02 5.24E-02 5.18E-02 0.048

ppm 2.08E+01 2.87E+01 2.85E+01 26.000

ppm@7%O2 2.21E+01 2.99E+01 2.94E+01 27.133

Tuesday, February 15, 2011 Page 16 of 22
9/30/2010

Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input 10910 MMBtu/hr 0 M23 Run 1

2 Heat Input 11371 MMBtu/hr 0 M23 Run 2

3 Heat Input 11289 MMBtu/hr 0 M23 Run 3

4 Heat Input 10229 MMBtu/hr 0 M26a Run 1

5 Heat Input 11258 MMBtu/hr 0 M26a Run 2

6 Heat Input 11295 MMBtu/hr 0 M26a Run 3

1 Steam Output 0 klb/hr 0

2 Steam Output 0 klb/hr 0

3 Steam Output 0 klb/hr 0

4 Steam Output 0 klb/hr 0

5 Steam Output 0 klb/hr 0

6 Steam Output 0 klb/hr 0

1 Gross Electric Generation 1201 MW 0 M23 Run 1

2 Gross Electric Generation 1266 MW 0 M23 Run 2

3 Gross Electric Generation 1271 MW 0 M23 Run 3

4 Gross Electric Generation 1116 MW 0 M26a Run 1

5 Gross Electric Generation 1262 MW 0 M26a Run 2

6 Gross Electric Generation 1268 MW 0 M26a Run 3

Run Name Value UOM Comments

Target

Value

1 ELECTROSTATIC PRECIPITATOR 0 0

1 LOW NOX BURNERS 0 0

1 WET SCRUBBER 0 0

1 SCR (SELECTIVE CATALYTIC REDUCTION) 0 0

1 DRY SORBENT INJECTION 0 0

Tuesday, February 15, 2011 Page 17 of 22
9/30/2010

Sampling / Stack Data Results Detail

Location Stack - Method 23

Average

Run Number 1 2 3

Test Date 6/10/2010 6/17/2010 6/18/2010

Run Start Time 10:30:00 AM 8:41:00 AM 8:42:00 AM

Run Finish Time 9:16:00 PM 6:43:00 PM 6:44:00 PM

Net Traversing Points 48 48 48

Net Run Time, minutes 576 576 576

Nozzle Diameter, inches 0.1895 0.1878 0.1878 0.188

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.009 1.009 1.009 1.009

Barometric Pressure, inches of Mercury 29.105 29.18 29.16 29.148

Average Orifice Meter Differential, inches H2O 1.15 7.70 1.23 3.360

Dry Gas Meter Volume Sampled, cubic feet 344.110 345.702 352.656 347.489

Average Dry Gas Meter Temperature, °F 110.52 108.29 112.94 110.583

Dry Gas Meter Volume Sampled, dscf 313.485 322.201 320.581 318.756

Total Moisture Liquid collected, g 1333.3 1346.1 1413.4 1,364.267

Volume of Water Vapor, standard cubic feet 62.76 63.36 66.53 64.217

Moisture Content of Stack Gas, % 16.68 16.43 17.19 16.767

Moisture Saturation at Stack Gas Temperature, % 15.53 15.06 15.40 15.330

Dry Mole Fraction 0.8447 0.8494 0.846 0.847

Carbon Dioxide, % 11.95 11.67 11.84 11.820

Oxygen, % 7.39 7.43 7.47 7.430

Carbon Monoxide & Nitrogen, % 80.66 80.9 80.69 80.750

Fuel Factor 1.13 1.15 1.13

Dry Molecular Weight, lb/lb-Mole 30.21 30.16 30.19 30.187

Wet Molecular weight, lb/lb-Mole 28.52 28.58 28.63 28.577

Flue Gas Static Pressure, inches of H2O -1 -1 -1 -1.000

Absolute Flue Gas Pressure, inches of Mercury 29.03 29.11 29.09 29.077

Average Stack Gas Temperature, °F 129.92 128.88 129.69 129.497

Average Velocity Head, inches of H2O 1.1416281530

6247

1.205719291

84543

1.222302094

60131

1.190

Average Stack Gas Velocity, feet/second 64.77 66.34 66.81 65.973

Stack Cross-Sectional Area, square feet 1,164.156 1,164.156 1,164.156 1,164.156

Dry Volumetric Flow Rate, dry scfm 3,318,677.7 3,433,506.6 3,436,897.3 3,396,360.5

33

Actual Wet Volumetric Flue Gas Flow Rate, acfm 4,524,143.0 4,633,806.5 4,666,635.7 4,608,195.0

67

Percent Isokinetic of Sampling Rate, % 97.5 98.6 98.0 98.033

Percent Excess Air, % 53.1 53.3 54.0 53.467

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

Round Duct Diameter, inches 462 462 462

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

Tuesday, February 15, 2011 Page 18 of 22
9/30/2010

Location Stack - 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

Tuesday, February 15, 2011 Page 19 of 22
9/30/2010

Location Stack - Method 3A CO2

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

Tuesday, February 15, 2011 Page 20 of 22
9/30/2010

Location Stack - Method 3A O2

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

Tuesday, February 15, 2011 Page 21 of 22
9/30/2010

Location Stack - 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

Tuesday, February 15, 2011 Page 22 of 22
9/30/2010

Location Stack - 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

Tuesday, February 15, 2011 Page 23 of 22