Name:

Title:

Company:

Sign Date:

Name:

Title:

Company:

Sign Date:

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.

Wednesday, February 02, 2011 Page 1 of 37
Facility Information:

NC_GG Allen Units 3,4

253 Plant Allen Road

Belmont NC 28012

Contact: Jon Hays

Phone: 317-838-4445

Fax: 317-8382490

Email: jon.hays@duke.energy.com

Testing Company:

AECOM

2 Technology Park Drive

Westford MA 01886

Contact: Patrick Ford

Phone: 978-589-3427

Fax: 978-589-3100

Email: pat.ford@aecom.com

Air Permit Number:

3757T31

Permitted Source ID/Name:

Units 3,4 No. 2 Fuel Oil/Coal-Fired Electric Utility Boilers

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:

This description should describe the process and associated controls to differentiate this facility from, or document 

similarity with others of same SCC.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 3707100039 FRS #: 3600039

SCC / Description 10100211 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Wet Bottom (Tangential) (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 354 0 0 0 8 2 4 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Exit % H2O Method 1 - 4 3 60 0

Stack Exit Carbon Monoxide Method 10 4 120 0

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 4 120 0

Stack Exit Hydrogen Fluoride Method 26A 3 60 0

Stack Exit Hydrogen Chloride Method 26A 3 60 0

Stack Exit Arsenic Method 29 3 180 0

Stack Exit Manganese Method 29 3 180 0

Wednesday, February 02, 2011 Page 2 of 37
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.

EPA Method 26A was modified to include the provisions cited in Method CTM-033 to allow simultaneous collection 

of HCl, HF and HCN. Modification included elimination of the 0.1 N H2SO4 impingers, addition of a third NaOH 

impinger and use of high normality NaOH absorbing solutions (6N in the 1st impinger and 2 N in the second and 

third) in order to maintain the pH of the solution high enough to prevent poor HCN analyte collection. The sample 

time was also reduced to 1-hour as allowed by EPA (see FAQ's section on the ICR website) again to ensure that the 

pH of the absorbing solution remained high.

Stack Exit Lead Method 29 3 180 0

Stack Exit Antimony Method 29 3 180 0

Stack Exit Beryllium Method 29 3 180 0

Stack Exit Cobalt Method 29 3 180 0

Stack Exit Chromium Method 29 3 180 0

Stack Exit Selenium Method 29 3 180 0

Stack Exit Cadmium Method 29 3 180 0

Stack Exit Nickel Method 29 3 180 0

Stack Exit O2 Method 3A O2 3 60 0

Stack Exit Co2 Method 3A CO2 3 60 0

Stack Exit Total Particulate Method 5/OTM-28 3 180 0

Stack Exit Filterable Particulate Method 5/OTM-28 3 180 0

Organic Condensible 

Particulate

Stack Exit Method 5/OTM-28 3 180 0

Inorganic (Aqueous) 

Condensible Part.

Stack Exit Method 5/OTM-28 3 180 0

Stack Exit Sulfur Dioxide Method 6C 3 60 0

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

Wednesday, February 02, 2011 Page 3 of 37
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 10 3

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, February 02, 2011 Page 4 of 37
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 25A 3

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, February 02, 2011 Page 5 of 37
Location Stack Exit - Method 26A

Average

Run Number CTM033-1 CTM033-2 CTM033-3

Test Date 3/17/2010 3/17/2010 3/18/2010

Run Start Time 4:50:00 PM 6:39:00 

PM

8:45:00 AM

Run Finish Time 6:00:00 PM 7:44:00 

PM

9:52:00 AM

Net Run Time, minutes 60 60 60

Dry Gas Meter Volume Sampled, dscf 38.093 38.173 38.999 38.422

Moisture Content of Stack Gas, % 15.71 15.76 15.69 15.720

Moisture Saturation at Stack Gas Temperature, % 14.06 13.92 13.78 13.920

Carbon Dioxide, % 13.83 13.93 13.95 13.903

Oxygen, % 5.61 5.5 5.38 5.497

Average Stack Gas Temperature, °F 126.29 125.92 126.42 126.210

Dry Volumetric Flow Rate, dry scfm 1,203,402.4 1,197,466.

8

1,218,049.6 1,206,306.26

7

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,599,783.7 1,588,301.

0

1,576,408.3 1,588,164.33

3

Percent Isokinetic of Sampling Rate, % 102.5 103.2 103.7 103.133

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

Wednesday, February 02, 2011 Page 6 of 37
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 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

Wednesday, February 02, 2011 Page 7 of 37
Location Stack Exit - Method 3A CO2 3

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 3A CO2 3 6

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, February 02, 2011 Page 8 of 37
Location Stack Exit - 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 Exit - Method 3A O2 3

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, February 02, 2011 Page 9 of 37
Location Stack Exit - Method 3A O2 3 6

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 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, February 02, 2011 Page 10 of 37
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 6C 3

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, February 02, 2011 Page 11 of 37
Location Stack Exit - Method 7E

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack Exit - Method 7E 3

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, February 02, 2011 Page 12 of 37
Emissions Summary

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

Elb/hr 2.30E+03 2.16E+03 1.17E+03 1,876.667

lb/mmBtuO2 4.26E-01 3.82E-01 2.16E-01 0.341

ppm 4.39E+02 3.95E+02 2.21E+02 351.667

ppm@7%O2 3.99E+02 3.57E+02 2.02E+02 319.333

Location: Stack Exit - Method 10 3

Compound: Carbon Monoxide

Average

Run 4

Elb/hr 1.37E+03 1,370.000

lb/mmBtuO2 2.48E-01 0.248

ppm 2.54E+02 254.000

ppm@7%O2 2.32E+02 232.000

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 8.77E-04 3.44E-04 4.25E-04 0.001

ppm 5.73E-01 2.26E-01 2.77E-01 0.359

ppm@7%O2 5.21E-01 2.05E-01 2.53E-01 0.326

Location: Stack Exit - Method 25A 3

Compound: Total organic compounds (TOC) as 

Average

Run 4

lb/mmBtuO2 6.48E-04 0.001

ppm 4.22E-01 0.422

ppm@7%O2 3.85E-01 0.385

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber CTM033-1 CTM033-2 CTM033-3

Mass_mg 1.305 1.535 1.331 1.390

Elb/hr 5.45E+00 6.37E+00 5.50E+00 5.773

lb/mmBtuO2 1.01E-03 1.18E-03 9.91E-04 0.001

mg/dscm 1.21E+00 1.42E+00 1.21E+00 1.280

mg/dscm@7%O2 1.10E+00 1.28E+00 1.08E+00 1.153

Compound: Hydrogen Fluoride

Average

RunNumber CTM033-1 CTM033-2 CTM033-3

Mass_mg 0.65 0.62 0.64 0.637

Elb/hr 2.72E+00 2.57E+00 2.64E+00 2.643

Wednesday, February 02, 2011 Page 13 of 37
lb/mmBtuO2 5.03E-04 4.75E-04 4.76E-04 0.000

mg/dscm 6.03E-01 5.74E-01 5.80E-01 0.586

mg/dscm@7%O2 5.48E-01 5.18E-01 5.19E-01 0.528

Location: Stack Exit - Method 29

Compound: Antimony

Average

RunNumber M29- R1 M29-R2 M29-R3

Mass_mg 0.00027 0.00041 0.00022 0.000

Elb/hr 3.08E-04 4.71E-04 2.51E-04 0.000

lb/mmBtuO2 5.61E-08 8.54E-08 4.42E-08 0.000

ug/dscm 6.69E-02 1.03E-01 5.37E-02 0.075

ug/dscm@7%O2 6.11E-02 9.30E-02 4.82E-02 0.067

Compound: Arsenic

Average

RunNumber M29- R1 M29-R2 M29-R3

Mass_mg 0.00254 0.0039 0.0042 0.004

Elb/hr 2.90E-03 4.48E-03 4.79E-03 0.004

lb/mmBtuO2 5.27E-07 8.13E-07 8.44E-07 0.000

ug/dscm 6.30E-01 9.81E-01 1.02E+00 0.877

ug/dscm@7%O2 5.75E-01 8.85E-01 9.15E-01 0.792

Compound: Beryllium

Average

RunNumber M29- R1 M29-R2 M29-R3

Mass_mg 0.00011 0.00008 0.00008 0.000

Elb/hr 1.25E-04 9.19E-05 9.13E-05 0.000

lb/mmBtuO2 2.28E-08 1.67E-08 1.61E-08 0.000

ug/dscm 2.73E-02 2.01E-02 1.95E-02 0.022

ug/dscm@7%O2 2.49E-02 1.81E-02 1.75E-02 0.020

Compound: Cadmium

Average

RunNumber M29- R1 M29-R2 M29-R3

Mass_mg 0.00058 0.00054 0.00018 0.000

Elb/hr 6.61E-04 6.20E-04 2.05E-04 0.000

lb/mmBtuO2 1.20E-07 1.13E-07 3.62E-08 0.000

ug/dscm 1.44E-01 1.36E-01 4.39E-02 0.108

ug/dscm@7%O2 1.31E-01 1.23E-01 3.94E-02 0.098

Compound: Chromium

Average

RunNumber M29- R1 M29-R2 M29-R3

Mass_mg 0.0112 0.0259 0.0137 0.017

Elb/hr 1.28E-02 2.98E-02 1.56E-02 0.019

lb/mmBtuO2 2.33E-06 5.40E-06 2.75E-06 0.000

ug/dscm 2.78E+00 6.51E+00 3.34E+00 4.210

ug/dscm@7%O2 2.54E+00 5.88E+00 3.00E+00 3.807

Compound: Cobalt

Average

RunNumber M29- R1 M29-R2 M29-R3

Wednesday, February 02, 2011 Page 14 of 37
Mass_mg 0.00055 0.00069 0.0006 0.001

Elb/hr 6.27E-04 7.93E-04 6.85E-04 0.001

lb/mmBtuO2 1.14E-07 1.44E-07 1.21E-07 0.000

ug/dscm 1.36E-01 1.74E-01 1.46E-01 0.152

ug/dscm@7%O2 1.24E-01 1.57E-01 1.31E-01 0.137

Compound: Lead

Average

RunNumber M29- R1 M29-R2 M29-R3

Mass_mg 0.00287 0.00336 0.00146 0.003

Elb/hr 3.27E-03 3.86E-03 1.67E-03 0.003

lb/mmBtuO2 5.96E-07 7.00E-07 2.93E-07 0.000

ug/dscm 7.11E-01 8.45E-01 3.56E-01 0.637

ug/dscm@7%O2 6.49E-01 7.63E-01 3.19E-01 0.577

Compound: Manganese

Average

RunNumber M29- R1 M29-R2 M29-R3

Mass_mg 0.011 0.0141 0.0111 0.012

Elb/hr 1.25E-02 1.62E-02 1.27E-02 0.014

lb/mmBtuO2 2.28E-06 2.94E-06 2.23E-06 0.000

ug/dscm 2.73E+00 3.55E+00 2.71E+00 2.997

ug/dscm@7%O2 2.49E+00 3.20E+00 2.43E+00 2.707

Compound: Nickel

Average

RunNumber M29- R1 M29-R2 M29-R3

Mass_mg 0.0105 0.03693 0.0134 0.020

Elb/hr 1.20E-02 4.24E-02 1.53E-02 0.023

lb/mmBtuO2 2.18E-06 7.69E-06 2.69E-06 0.000

ug/dscm 2.60E+00 9.29E+00 3.27E+00 5.053

ug/dscm@7%O2 2.37E+00 8.39E+00 2.93E+00 4.563

Compound: Selenium

Average

RunNumber M29- R1 M29-R2 M29-R3

Mass_mg 0.0732 0.1426 0.1309 0.116

Elb/hr 8.35E-02 1.64E-01 1.49E-01 0.132

lb/mmBtuO2 1.52E-05 2.97E-05 2.63E-05 0.000

ug/dscm 1.81E+01 3.59E+01 3.19E+01 28.633

ug/dscm@7%O2 1.65E+01 3.24E+01 2.86E+01 25.833

Location: Stack Exit - Method 5/OTM-28

Compound: Filterable Particulate

Average

RunNumber M5-R1 M5-R2 M5-R3

Mass_mg 15.9 19.8 23.3 19.667

Elb/hr 1.93E+01 2.38E+01 2.80E+01 23.700

gr/dscf 1.77E-03 2.18E-03 2.55E-03 0.002

gr/dscf@7%O2 1.62E-03 1.97E-03 2.29E-03 0.002

lb/mmBtuO2 3.39E-03 4.13E-03 4.82E-03 0.004

Wednesday, February 02, 2011 Page 15 of 37
Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber M5-R1 M5-R2 M5-R3

Mass_mg 17 7.4 6.4 10.267

Elb/hr 2.07E+01 8.91E+00 7.68E+00 12.430

gr/dscf 1.89E-03 8.14E-04 7.02E-04 0.001

gr/dscf@7%O2 1.72E-03 7.35E-04 6.30E-04 0.001

lb/mmBtuO2 3.62E-03 1.54E-03 1.32E-03 0.002

Compound: Organic Condensible Particulate

Average

RunNumber M5-R1 M5-R2 M5-R3

Mass_mg 7.4 6.3 8.5 7.400

Elb/hr 9.00E+00 7.59E+00 1.02E+01 8.930

gr/dscf 8.22E-04 6.93E-04 9.32E-04 0.001

gr/dscf@7%O2 7.50E-04 6.26E-04 8.36E-04 0.001

lb/mmBtuO2 1.58E-03 1.31E-03 1.76E-03 0.002

Compound: Total Particulate

Average

RunNumber M5-R1 M5-R2 M5-R3

Mass_mg 40.3 33.5 38.2 37.333

Elb/hr 4.90E+01 4.03E+01 4.58E+01 45.033

gr/dscf 4.48E-03 3.69E-03 4.19E-03 0.004

gr/dscf@7%O2 4.09E-03 3.33E-03 3.76E-03 0.004

lb/mmBtuO2 8.58E-03 6.99E-03 7.89E-03 0.008

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Run CTM033-1 CTM033-2 CTM033-3

Elb/hr 7.20E+02 7.28E+02 7.21E+02 723.000

lb/mmBtuO2 1.32E-01 1.33E-01 1.29E-01 0.131

ppm 5.96E+01 6.04E+01 5.89E+01 59.633

ppm@7%O2 5.42E+01 5.45E+01 5.28E+01 53.833

Location: Stack Exit - Method 6C 3

Compound: Sulfur Dioxide

Average

Run Organic-1 Organic-2 Organic-3

Elb/hr 3.42E+02 4.41E+02 2.69E+02 350.667

lb/mmBtuO2 6.09E-02 7.85E-02 4.82E-02 0.063

ppm 2.74E+01 3.55E+01 2.16E+01 28.167

ppm@7%O2 2.49E+01 3.21E+01 1.97E+01 25.567

Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run CTM033-1 CTM033-2 CTM033-3

Elb/hr 9.04E+02 9.02E+02 9.35E+02 913.667

lb/mmBtuO2 1.66E-01 1.65E-01 1.67E-01 0.166

ppm 1.04E+02 1.04E+02 1.06E+02 104.667

Wednesday, February 02, 2011 Page 16 of 37
Process Run Data

ppm@7%O2 9.45E+01 9.39E+01 9.49E+01 94.433

Location: Stack Exit - Method 7E 3

Compound: Nitrogen oxides (NOx)

Average

Run Organic-1 Organic-2 Organic-3

Elb/hr 9.64E+02 9.61E+02 9.62E+02 962.333

lb/mmBtuO2 1.72E-01 1.71E-01 1.73E-01 0.172

ppm 1.07E+02 1.08E+02 1.08E+02 107.667

ppm@7%O2 9.73E+01 9.77E+01 9.86E+01 97.867

Wednesday, February 02, 2011 Page 17 of 37
Process Run Data

Run Name Value UOM Comments

Target

Value

1 Bituminous Coal Burned Tons/million BTU using O2 0 0

2 Bituminous Coal Burned Tons/million BTU using O2 0 0

3 Bituminous Coal Burned Tons/million BTU using O2 0 0

4 Bituminous Coal Burned Tons/million BTU using O2 0 0

1 Average Heat Input 0 MMBtu/hr 0

2 Average Heat Input 0 MMBtu/hr 0

3 Average Heat Input 0 MMBtu/hr 0

4 Average Heat Input 0 MMBtu/hr 0

1 Steam Output 0 1000 lb steam/hr 0

2 Steam Output 0 1000 lb steam/hr 0

3 Steam Output 0 1000 lb steam/hr 0

4 Steam Output 0 1000 lb steam/hr 0

1 Synfuel Firing Rate 0 1000 Tons/hr 0

2 Synfuel Firing Rate 0 1000 Tons/hr 0

3 Synfuel Firing Rate 0 1000 Tons/hr 0

4 Synfuel Firing Rate 0 1000 Tons/hr 0

1 Petroleum Coke Firing Rate 0 1000 Tons/hr 0

2 Petroleum Coke Firing Rate 0 1000 Tons/hr 0

3 Petroleum Coke Firing Rate 0 1000 Tons/hr 0

4 Petroleum Coke Firing Rate 0 1000 Tons/hr 0

1 Coal Gas Firing Rate 0 Ft^3/min 0

2 Coal Gas Firing Rate 0 Ft^3/min 0

3 Coal Gas Firing Rate 0 Ft^3/min 0

4 Coal Gas Firing Rate 0 Ft^3/min 0

1 Fuel Oil Firing Rate 0 gal/hr 0

2 Fuel Oil Firing Rate 0 gal/hr 0

3 Fuel Oil Firing Rate 0 gal/hr 0

4 Fuel Oil Firing Rate 0 gal/hr 0

1 Flue Gas Flow Rate 0 0

4 Flue Gas Flow Rate 0 0

1 Pressure Drop Across FGD (if applicable) 0 in H20 0

4 Pressure Drop Across FGD (if applicable) 0 in H20 0

1 FGD Scrubber Liquor pH 0 pH 0

Wednesday, February 02, 2011 Page 18 of 37
APCD Run Data

Process Lab Run Data

4 FGD Scrubber Liquor pH 0 pH 0

1 FGD Scrubber Liquor Flow Rate 0 gal/min 0

4 FGD Scrubber Liquor Flow Rate 0 gal/min 0

1 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

4 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

1 Flue Gas Oxygen Content 0 % 0

4 Flue Gas Oxygen Content 0 % 0

1 Flue Gas Carbon Dioxide Content 0 % 0

4 Flue Gas Carbon Dioxide Content 0 % 0

1 Flue Gas Moisture Content 0 % 0

4 Flue Gas Moisture Content 0 % 0

1 Flue Gas Sampling Point Temperature 0 Deg F 0

4 Flue Gas Sampling Point Temperature 0 Deg F 0

1 Flue Gas Pressure 0 atm 0

4 Flue Gas Pressure 0 atm 0

1 Standard Pressure 0 atm 0

4 Standard Pressure 0 atm 0

1 Standard Temperature 0 Deg F 0

4 Standard Temperature 0 Deg F 0

1 Unit Gross Electrical Output 0 Mwe 0

4 Unit Gross Electrical Output 0 Mwe 0

1 Unit Net Electric Generation 0 MWh 0

4 Unit Net Electric Generation 0 MWh 0

Run Name Value UOM Comments

Target

Value

1 List all emissions control devices in order of 

process flow. Choose from

0 0

1 drop down lists. If not on list add description and 

provide detailed

0 0

1 desription in section 5a. 0 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value 0 Btu/lb

1 Fuel Moisture 0 %

Wednesday, February 02, 2011 Page 19 of 37
1 Ultimate/Proximate Analysis 0

1 Fuel Chlorine Content 0 mg/kg

1 Fuel Fluorine Content 0 mg/kg

1 Metals Content 0 mg/kg

Wednesday, February 02, 2011 Page 20 of 37
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, February 02, 2011 Page 21 of 37
Location Stack Exit - Method 10 3

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, February 02, 2011 Page 22 of 37
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, February 02, 2011 Page 23 of 37
Location Stack Exit - Method 25A 3

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, February 02, 2011 Page 24 of 37
Location Stack Exit - Method 26A

Average

Run Number CTM033-1 CTM033-2 CTM033-3

Test Date 3/17/2010 3/17/2010 3/18/2010

Run Start Time 4:50:00 PM 6:39:00 PM 8:45:00 AM

Run Finish Time 6:00:00 PM 7:44:00 PM 9:52:00 AM

Net Traversing Points 24 24 24

Net Run Time, minutes 60 60 60

Nozzle Diameter, inches 0.254 0.254 0.254 0.254

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.004 1.004 1.004 1.004

Barometric Pressure, inches of Mercury 29.1 29.1 29.8 29.333

Average Orifice Meter Differential, inches H2O 1.44 1.43 1.43 1.433

Dry Gas Meter Volume Sampled, cubic feet 40.273 40.783 40.077 40.378

Average Dry Gas Meter Temperature, °F 87.08 92.83 84.50 88.137

Dry Gas Meter Volume Sampled, dscf 38.093 38.173 38.999 38.422

Total Moisture Liquid collected, g 150.8 151.7 154.2 152.233

Volume of Water Vapor, standard cubic feet 7.10 7.14 7.26 7.167

Moisture Content of Stack Gas, % 15.71 15.76 15.69 15.720

Moisture Saturation at Stack Gas Temperature, % 14.06 13.92 13.78 13.920

Dry Mole Fraction 0.8594 0.8608 0.8622 0.861

Carbon Dioxide, % 13.83 13.93 13.95 13.903

Oxygen, % 5.61 5.5 5.38 5.497

Carbon Monoxide & Nitrogen, % 80.56 80.57 80.67 80.600

Fuel Factor 1.11 1.11 1.11

Dry Molecular Weight, lb/lb-Mole 30.44 30.45 30.45 30.447

Wet Molecular weight, lb/lb-Mole 28.99 29.05 29.08 29.040

Flue Gas Static Pressure, inches of H2O -0.26 -0.26 -0.25 -0.257

Absolute Flue Gas Pressure, inches of Mercury 29.08 29.08 29.78 29.313

Average Stack Gas Temperature, °F 126.29 125.92 126.42 126.210

Average Velocity Head, inches of H2O 0.4242966609

68342

0.419467178

61162

0.423242929

711302

0.422

Average Stack Gas Velocity, feet/second 39.01 38.73 38.44 38.727

Stack Cross-Sectional Area, square feet 683.493 683.493 683.493 683.493

Dry Volumetric Flow Rate, dry scfm 1,203,402.4 1,197,466.8 1,218,049.6 1,206,306.2

67

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,599,783.7 1,588,301.0 1,576,408.3 1,588,164.3

33

Percent Isokinetic of Sampling Rate, % 102.5 103.2 103.7 103.133

Percent Excess Air, % 35.8 34.9 33.8 34.833

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

Round Duct Diameter, inches 354 354 354

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, February 02, 2011 Page 25 of 37
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, February 02, 2011 Page 26 of 37
Location Stack Exit - 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

Wednesday, February 02, 2011 Page 27 of 37
Location Stack Exit - Method 3A CO2 3

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, February 02, 2011 Page 28 of 37
Location Stack Exit - Method 3A CO2 3 6

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, February 02, 2011 Page 29 of 37
Location Stack Exit - 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

Wednesday, February 02, 2011 Page 30 of 37
Location Stack Exit - Method 3A O2 3

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, February 02, 2011 Page 31 of 37
Location Stack Exit - Method 3A O2 3 6

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, February 02, 2011 Page 32 of 37
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, February 02, 2011 Page 33 of 37
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, February 02, 2011 Page 34 of 37
Location Stack Exit - Method 6C 3

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, February 02, 2011 Page 35 of 37
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, February 02, 2011 Page 36 of 37
Location Stack Exit - Method 7E 3

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, February 02, 2011 Page 37 of 37