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 09, 2011 Page 1 of 19
Facility Information:

Gulf Power-Plant Scholz

1460 Gulf Power Rd

Sneads Fl 32460

Contact:

Phone:

Fax:

Email:

Testing Company:

Weston Solutions

1625 Pumphrey Ave

Auburn Al 36832

Contact:Jon Howard

Phone: 334-466-5600

Fax: 334-466-5666

Email: j.howard@westonsolutions.com

Air Permit Number: Permitted Source ID/Name:

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:

See Attached Report

Industry/SCC/NAIS

Sampling Location Information:

Test Parameter Information:

AFS #: FRS #:

SCC / Description

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 162 0 0 0 300 936 4 24

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Carbon Monoxide Method 10 3 0

Stack Formaldehyde Method 0011 3 0

Total organic compounds 

(TOC) as Propane

Stack Method 25A 3 0

Stack Hydrogen Chloride Method 26A 3 0

Stack Hydrogen Fluoride Method 26A 3 0

Inorganic (Aqueous) 

Condensible Part.

Stack OTM - 27/28 3 0

Wednesday, February 09, 2011 Page 2 of 19
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.

See Attached Report

Organic Condensible 

Particulate

Stack OTM - 27/28 3 0

Stack Filterable PM2.5 OTM - 27/28 3 0

Stack Beryllium Method 29 0

Stack Filterable Particulate Method 29 0

Stack Cadmium Method 29 0

Stack Chromium Method 29 0

Stack Lead Method 29 0

Stack Manganese Method 29 0

Stack Nickel Method 29 0

Stack Selenium Method 29 0

Stack Antimony Method 29 0

Stack Cobalt Method 29 0

Stack Phosphorus (yellow or white) Method 29 0

Stack Arsenic Method 29 0

Stack O2 Method 3A O2 3 0

Stack Co2 Method 3A CO2 3 0

Wednesday, February 09, 2011 Page 3 of 19
Sampling / Stack Data Results Summary

Location Stack - Method 0011

Average

Run Number 1 2 3

Test Date 3/3/2010 3/3/2010 3/3/2010

Run Start Time 10:00:00 AM 1:40:00 PM 4:50:00 PM

Run Finish Time 12:28:00 PM 3:58:00 PM 7:03:00 PM

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 68.143 69.082 70.853 69.359

Moisture Content of Stack Gas, % 6.30 6.26 6.02 6.193

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

Carbon Dioxide, % 11.9 11.9 12 11.933

Oxygen, % 7.4 7.4 7.4 7.400

Average Stack Gas Temperature, °F 290.08 294.45 295.65 293.393

Dry Volumetric Flow Rate, dry scfm 280,092.5 282,323.6 286,558.3 282,991.467

Actual Wet Volumetric Flue Gas Flow Rate, acfm 429,245.2 434,999.4 441,097.1 435,113.900

Percent Isokinetic of Sampling Rate, % 100.6 101.2 102.2 101.333

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 - Method 10

Average

Run Number 1 2 3

Test Date 3/3/2010 3/3/2010 3/3/2010

Run Start Time 10:00:00 AM 1:39:00 PM 4:50:00 PM

Run Finish Time 12:28:00 PM 3:56:00 PM 7:04:00 PM

Carbon Dioxide, % 11.9 11.9 12 11.933

Oxygen, % 7.4 7.4 7.4 7.400

Dry Volumetric Flow Rate, dry scfm 279999 282242 286442 282,894.333

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

Moisture, % 6.3 6.3 6 6.200

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Wednesday, February 09, 2011 Page 4 of 19
Location Stack - Method 25A

Average

Run Number 1 2 3

Test Date 3/3/2010 3/3/2010 3/3/2010

Run Start Time 10:00:00 AM 1:39:00 PM 4:50:00 PM

Run Finish Time 12:28:00 PM 3:56:00 PM 7:04:00 PM

Carbon Dioxide, % 11.9 11.9 12 11.933

Oxygen, % 7.4 7.4 7.4 7.400

Dry Volumetric Flow Rate, dry scfm 279999 282242 286442 282,894.333

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

Moisture, % 6.3 6.3 6 6.200

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack - Method 26A

Average

Run Number 1 2 3

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

Run Start Time 7:15:00 AM 10:45:00 

AM

2:10:00 PM

Run Finish Time 10:31:00 AM 2:00:00 PM 5:22:00 PM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 108.233 105.496 102.327 105.352

Moisture Content of Stack Gas, % 6.78 6.73 6.68 6.730

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

Carbon Dioxide, % 12 12 12 12.000

Oxygen, % 7.2 7.1 7.1 7.133

Average Stack Gas Temperature, °F 285.95 293.10 296.53 291.860

Dry Volumetric Flow Rate, dry scfm 295,598.3 285,949.9 283,802.3 288,450.167

Actual Wet Volumetric Flue Gas Flow Rate, acfm 449,341.9 438,606.5 437,060.6 441,669.667

Percent Isokinetic of Sampling Rate, % 100.9 101.7 99.4 100.667

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 09, 2011 Page 5 of 19
Location Stack - Method 29

Average

Run Number 1 2 3

Test Date 3/9/2010 3/9/2010 3/10/2010

Run Start Time 7:51:00 AM 2:31:00 PM 7:45:00 AM

Run Finish Time 1:08:00 PM 9:02:00 PM 2:03:00 PM

Net Run Time, minutes 300 360 360

Dry Gas Meter Volume Sampled, dscf 172.143 201.792 209.692 194.542

Moisture Content of Stack Gas, % 6.94 6.36 7.10 6.800

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

Carbon Dioxide, % 11.3 11.4 11.6 11.433

Oxygen, % 7.8 7.6 7.6 7.667

Average Stack Gas Temperature, °F 303.10 304.63 303.63 303.787

Dry Volumetric Flow Rate, dry scfm 289,146.2 281,414.0 293,195.2 287,918.467

Actual Wet Volumetric Flue Gas Flow Rate, acfm 454,065.5 440,066.5 461,537.4 451,889.800

Percent Isokinetic of Sampling Rate, % 98.5 98.8 98.6 98.633

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 - Method 3A CO2

Average

Run Number 1 2 3

Test Date 3/3/2010 3/3/2010 3/3/2010

Run Start Time 10:00:00 AM 1:39:00 PM 4:50:00 PM

Run Finish Time 12:28:00 PM 3:56:00 PM 7:04:00 PM

Carbon Dioxide, % 11.9 11.9 12 11.933

Oxygen, % 7.4 7.4 7.4 7.400

Dry Volumetric Flow Rate, dry scfm 279999 282242 286442 282,894.333

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

Moisture, % 6.3 6.3 6 6.200

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Wednesday, February 09, 2011 Page 6 of 19
Location Stack - Method 3A O2

Average

Run Number 1 2 3

Test Date 3/3/2010 3/3/2010 3/3/2010

Run Start Time 10:00:00 AM 1:39:00 PM 4:50:00 PM

Run Finish Time 12:28:00 PM 3:56:00 PM 7:04:00 PM

Carbon Dioxide, % 11.9 11.9 12 11.933

Oxygen, % 7.4 7.4 7.4 7.400

Dry Volumetric Flow Rate, dry scfm 279999 282242 286442 282,894.333

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

Moisture, % 6.3 6.3 6 6.200

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack - OTM - 27/28

Average

Run Number 1 2 3

Test Date 3/9/2010 3/9/2010 3/10/2010

Run Start Time 7:51:00 AM 2:31:00 PM 7:45:00 AM

Run Finish Time 2:00:00 PM 8:52:00 PM 2:06:00 PM

Net Run Time, minutes 336.3 349.75 364

Dry Gas Meter Volume Sampled, dscf 119.982 126.480 130.327 125.596

Moisture Content of Stack Gas, % 6.35 5.74 7.05 6.380

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

Carbon Dioxide, % 11.3 11.4 11.6 11.433

Oxygen, % 7.8 7.6 7.6 7.667

Average Stack Gas Temperature, °F 300.49 302.89 301.74 301.707

Dry Volumetric Flow Rate, dry scfm 295,181.1 292,290.4 296,269.8 294,580.433

Actual Wet Volumetric Flue Gas Flow Rate, acfm 459,046.8 453,034.9 464,972.7 459,018.133

Percent Isokinetic of Sampling Rate, % 92.7 94.9 92.7 93.433

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 09, 2011 Page 7 of 19
Emissions Summary

Location: Stack - Method 0011

Compound: Formaldehyde

Average

RunNumber 1 2 3

Mass_mg 0.012 0.01 0.009 0.010

Elb/hr 6.52E-03 5.41E-03 4.81E-03 0.006

lb/mmBtuO2 5.88E-06 4.83E-06 4.24E-06 0.000

ppm 4.98E-03 4.09E-03 3.59E-03 0.004

ppm@7%O2 5.13E-03 4.21E-03 3.70E-03 0.004

Location: Stack - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 8.41E-02 1.04E-01 7.56E-02 0.088

ppm 7.64E+01 9.43E+01 6.87E+01 79.800

ppm@7%O2 7.87E+01 9.71E+01 7.07E+01 82.167

Location: Stack - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 3.44E-04 8.60E-04 1.03E-03 0.001

ppm 1.98E-01 4.96E-01 5.95E-01 0.430

ppm@7%O2 2.04E-01 5.11E-01 6.13E-01 0.443

Location: Stack - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 333 352 360 348.333

lb/mmBtuO2 1.01E-01 1.09E-01 1.15E-01 0.108

ppm 7.17E+01 7.77E+01 8.20E+01 77.133

ppm@7%O2 7.27E+01 7.83E+01 8.26E+01 77.867

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 18.6 19.1 19.7 19.133

lb/mmBtuO2 5.65E-03 5.91E-03 6.29E-03 0.006

ppm 7.30E+00 7.69E+00 8.17E+00 7.720

ppm@7%O2 7.41E+00 7.75E+00 8.23E+00 7.797

Location: Stack - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.0088 0.0088 0.00891 0.009

lb/mmBtuO2 1.76E-06 1.48E-06 1.44E-06 0.000

Wednesday, February 09, 2011 Page 8 of 19
Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.02045 0.02415 0.02515 0.023

lb/mmBtuO2 4.09E-06 4.05E-06 4.06E-06 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.0024 0.00259 0.00253 0.003

lb/mmBtuO2 4.80E-07 4.35E-07 4.09E-07 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.0022 0.0022 0.0022 0.002

lb/mmBtuO2 4.40E-07 3.69E-07 3.55E-07 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.01286 0.01497 0.01629 0.015

lb/mmBtuO2 2.57E-06 2.51E-06 2.63E-06 0.000

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.00338 0.00387 0.00409 0.004

lb/mmBtuO2 6.75E-07 6.50E-07 6.61E-07 0.000

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 19 23 27 23.000

lb/mmBtuO2 3.80E-03 3.86E-03 4.36E-03 0.004

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.00775 0.00886 0.00972 0.009

lb/mmBtuO2 1.55E-06 1.49E-06 1.57E-06 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.0181 0.0204 0.0213 0.020

lb/mmBtuO2 3.62E-06 3.43E-06 3.44E-06 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.01802 0.01642 0.01692 0.017

lb/mmBtuO2 3.60E-06 2.76E-06 2.73E-06 0.000

Wednesday, February 09, 2011 Page 9 of 19
Process Run Data

Compound: Phosphorus (yellow or white)

Average

RunNumber 1 2 3

Mass_mg 0.040805 0.046805 0.031805 0.040

lb/mmBtuO2 8.15E-06 7.86E-06 5.14E-06 0.000

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.3776 0.4338 0.4362 0.416

lb/mmBtuO2 7.55E-05 7.28E-05 7.05E-05 0.000

Location: Stack - OTM - 27/28

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 5.7 6 5.5 5.733

lb/mmBtuO2 1.63E-03 1.61E-03 1.43E-03 0.002

mg/dscm 1.68E+00 1.68E+00 1.49E+00 1.617

mg/dscm@7%O2 1.78E+00 1.76E+00 1.56E+00 1.700

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 39.1 37.5 40.8 39.133

lb/mmBtuO2 1.12E-02 1.00E-02 1.06E-02 0.011

mg/dscm 1.15E+01 1.05E+01 1.11E+01 11.033

mg/dscm@7%O2 1.22E+01 1.10E+01 1.16E+01 11.600

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 5 11.4 16.3 10.900

lb/mmBtuO2 1.43E-03 3.05E-03 4.24E-03 0.003

mg/dscm 1.47E+00 3.18E+00 4.42E+00 3.023

mg/dscm@7%O2 1.56E+00 3.32E+00 4.62E+00 3.167

Wednesday, February 09, 2011 Page 10 of 19
Process Run Data

APCD Run Data

Process Lab Run Data

Wednesday, February 09, 2011 Page 11 of 19
Sampling / Stack Data Results Detail

Location Stack - Method 0011

Average

Run Number 1 2 3

Test Date 3/3/2010 3/3/2010 3/3/2010

Run Start Time 10:00:00 AM 1:40:00 PM 4:50:00 PM

Run Finish Time 12:28:00 PM 3:58:00 PM 7:03:00 PM

Net Traversing Points 40 40 40

Net Run Time, minutes 120 120 120

Nozzle Diameter, inches 0.23 0.23 0.23 0.230

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.006 1.006 1.006 1.006

Barometric Pressure, inches of Mercury 29.64 29.64 29.64 29.640

Average Orifice Meter Differential, inches H2O 1.05 1.09 1.13 1.090

Dry Gas Meter Volume Sampled, cubic feet 69.620 70.314 72.190 70.708

Average Dry Gas Meter Temperature, °F 79.00 77.03 77.63 77.887

Dry Gas Meter Volume Sampled, dscf 68.143 69.082 70.853 69.359

Total Moisture Liquid collected, g 97.200000000

0004

97.90000000

00001

96.40000000

00001

97.167

Volume of Water Vapor, standard cubic feet 4.58 4.61 4.54 4.577

Moisture Content of Stack Gas, % 6.30 6.26 6.02 6.193

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

Dry Mole Fraction 0.937 0.9374 0.9398 0.938

Carbon Dioxide, % 11.9 11.9 12 11.933

Oxygen, % 7.4 7.4 7.4 7.400

Carbon Monoxide & Nitrogen, % 80.7 80.7 80.6 80.667

Fuel Factor 1.13 1.13 1.13

Dry Molecular Weight, lb/lb-Mole 30.20 30.20 30.22 30.207

Wet Molecular weight, lb/lb-Mole 29.43 29.44 29.48 29.450

Flue Gas Static Pressure, inches of H2O -0.5 -0.5 -0.5 -0.500

Absolute Flue Gas Pressure, inches of Mercury 29.60 29.60 29.60 29.600

Average Stack Gas Temperature, °F 290.08 294.45 295.65 293.393

Average Velocity Head, inches of H2O 0.5625577664

02107

0.574556414

036456

0.590644887

423956

0.576

Average Stack Gas Velocity, feet/second 49.98 50.65 51.36 50.663

Stack Cross-Sectional Area, square feet 143.139 143.139 143.139 143.139

Dry Volumetric Flow Rate, dry scfm 280,092.5 282,323.6 286,558.3 282,991.467

Actual Wet Volumetric Flue Gas Flow Rate, acfm 429,245.2 434,999.4 441,097.1 435,113.900

Percent Isokinetic of Sampling Rate, % 100.6 101.2 102.2 101.333

Percent Excess Air, % 53.2 53.2 53.3 53.233

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

Round Duct Diameter, inches 162 162 162

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 09, 2011 Page 12 of 19
Location Stack - Method 10

Average

Run Number 1 2 3

Test Date 3/3/2010 3/3/2010 3/3/2010

Run Start Time 10:00:00 AM 1:39:00 PM 4:50:00 PM

Run Finish Time 12:28:00 PM 3:56:00 PM 7:04:00 PM

Carbon Dioxide, % 11.9 11.9 12 11.933

Oxygen, % 7.4 7.4 7.4 7.400

Fuel Factor 1.13 1.13 1.13

Dry Volumetric Flow Rate, dry scfm 279999 282242 286442 282,894.333

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

Moisture, % 6.3 6.3 6 6.200

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 900 900 900 900.000

Operating Units ppm ppm ppm

No. Readings/Avg.

Calibration Set 3 3 3 3.000

Calibration Pre Zero Cylinder ID XC011677B XC011677B XC011677B

Calibration Pre Zero Cylinder Instrument Response 7 5 5 5.667

Calibration Pre Zero Cylinder Bias 0.22 0 0 0.073

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC125113 CC125113 CC125113

Calibration Pre High Cylinder Instrument Response 436 435 436 435.667

Calibration Pre High Cylinder Bias -1 -1.11 -1 -1.037

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID XC011677B XC011677B XC011677B

Calibration Post Zero Cylinder Instrument Response 5 5 5 5.000

Calibration Post Zero Cylinder Bias 0 0 0 0.000

Calibration Post Zero Cylinder Drift 0.22 0 0 0.073

Calibration Post High Cylinder ID CC125113 CC125113 CC125113

Calibration Post High Cylinder Instrument Response 435 436 437 436.000

Calibration Post High Cylinder Bias -1.11 -1 -0.89 -1.000

Calibration Post High Cylinder Drift 0.11 0.11 0.11 0.110

Cavg 78 94 70 80.667

Cavg Units ppmvd ppmvd ppmvd

Cgas 76.4424 94.2718 68.6906 79.802

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Wednesday, February 09, 2011 Page 13 of 19
Location Stack - Method 25A

Average

Run Number 1 2 3

Test Date 3/3/2010 3/3/2010 3/3/2010

Run Start Time 10:00:00 AM 1:39:00 PM 4:50:00 PM

Run Finish Time 12:28:00 PM 3:56:00 PM 7:04:00 PM

Carbon Dioxide, % 11.9 11.9 12 11.933

Oxygen, % 7.4 7.4 7.4 7.400

Fuel Factor 1.13 1.13 1.13

Dry Volumetric Flow Rate, dry scfm 279999 282242 286442 282,894.333

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

Moisture, % 6.3 6.3 6 6.200

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 25.1 25.1 25.1 25.100

Operating Units ppm ppm ppm

No. Readings/Avg.

Calibration Set 4 4 4 4.000

Calibration Pre Zero Cylinder ID XC011677B XC011677B XC011677B

Calibration Pre Zero Cylinder Instrument Response 0 0 0 0.000

Calibration Pre Zero Cylinder Bias 0 0 0 0.000

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC23540 CC23540 CC23540

Calibration Pre High Cylinder Instrument Response 12.5 12.5 12.5 12.500

Calibration Pre High Cylinder Bias 0 0 0 0.000

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID XC011677B XC011677B XC011677B

Calibration Post Zero Cylinder Instrument Response 0 0 0 0.000

Calibration Post Zero Cylinder Bias 0 0 0 0.000

Calibration Post Zero Cylinder Drift 0 0 0 0.000

Calibration Post High Cylinder ID CC23540 CC23540 CC23540

Calibration Post High Cylinder Instrument Response 12.5 12.5 12.5 12.500

Calibration Post High Cylinder Bias 0 0 0 0.000

Calibration Post High Cylinder Drift 0 0 0 0.000

Cavg 0.2 0.5 0.6 0.433

Cavg Units ppmvd ppmvd ppmvd

Cgas 0.1984 0.496 0.5952 0.430

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Wednesday, February 09, 2011 Page 14 of 19
Location Stack - Method 26A

Average

Run Number 1 2 3

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

Run Start Time 7:15:00 AM 10:45:00 AM 2:10:00 PM

Run Finish Time 10:31:00 AM 2:00:00 PM 5:22:00 PM

Net Traversing Points 40 40 40

Net Run Time, minutes 180 180 180

Nozzle Diameter, inches 0.23 0.23 0.23 0.230

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.981 0.981 0.981 0.981

Barometric Pressure, inches of Mercury 29.87 29.87 29.87 29.870

Average Orifice Meter Differential, inches H2O 1.24 1.19 1.17 1.200

Dry Gas Meter Volume Sampled, cubic feet 113.495 111.622 108.150 111.089

Average Dry Gas Meter Temperature, °F 83.90 88.73 88.10 86.910

Dry Gas Meter Volume Sampled, dscf 108.233 105.496 102.327 105.352

Total Moisture Liquid collected, g 167.19999999

9999

161.7 155.8 161.567

Volume of Water Vapor, standard cubic feet 7.87 7.61 7.33 7.603

Moisture Content of Stack Gas, % 6.78 6.73 6.68 6.730

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

Dry Mole Fraction 0.9322 0.9327 0.9332 0.933

Carbon Dioxide, % 12 12 12 12.000

Oxygen, % 7.2 7.1 7.1 7.133

Carbon Monoxide & Nitrogen, % 80.8 80.9 80.9 80.867

Fuel Factor 1.14 1.15 1.15

Dry Molecular Weight, lb/lb-Mole 30.21 30.20 30.20 30.203

Wet Molecular weight, lb/lb-Mole 29.38 29.38 29.39 29.383

Flue Gas Static Pressure, inches of H2O -0.52 -0.52 -0.52 -0.520

Absolute Flue Gas Pressure, inches of Mercury 29.83 29.83 29.83 29.830

Average Stack Gas Temperature, °F 285.95 293.10 296.53 291.860

Average Velocity Head, inches of H2O 0.6236647114

17803

0.588613575

550966

0.581861778

135292

0.598

Average Stack Gas Velocity, feet/second 52.32 51.07 50.89 51.427

Stack Cross-Sectional Area, square feet 143.139 143.139 143.139 143.139

Dry Volumetric Flow Rate, dry scfm 295,598.3 285,949.9 283,802.3 288,450.167

Actual Wet Volumetric Flue Gas Flow Rate, acfm 449,341.9 438,606.5 437,060.6 441,669.667

Percent Isokinetic of Sampling Rate, % 100.9 101.7 99.4 100.667

Percent Excess Air, % 51.0 49.8 49.8 50.200

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

Round Duct Diameter, inches 162 162 162

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 09, 2011 Page 15 of 19
Location Stack - Method 29

Average

Run Number 1 2 3

Test Date 3/9/2010 3/9/2010 3/10/2010

Run Start Time 7:51:00 AM 2:31:00 PM 7:45:00 AM

Run Finish Time 1:08:00 PM 9:02:00 PM 2:03:00 PM

Net Traversing Points 60 60 60

Net Run Time, minutes 300 360 360

Nozzle Diameter, inches 0.23 0.23 0.23 0.230

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.006 1.006 1.006 1.006

Barometric Pressure, inches of Mercury 29.6 29.6 29.6 29.600

Average Orifice Meter Differential, inches H2O 1.11 1.05 1.15 1.103

Dry Gas Meter Volume Sampled, cubic feet 176.927 207.235 215.844 200.002

Average Dry Gas Meter Temperature, °F 81.58 81.07 82.45 81.700

Dry Gas Meter Volume Sampled, dscf 172.143 201.792 209.692 194.542

Total Moisture Liquid collected, g 272.6 291.1 340.6 301.433

Volume of Water Vapor, standard cubic feet 12.83 13.70 16.03 14.187

Moisture Content of Stack Gas, % 6.94 6.36 7.10 6.800

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

Dry Mole Fraction 0.9306 0.9364 0.929 0.932

Carbon Dioxide, % 11.3 11.4 11.6 11.433

Oxygen, % 7.8 7.6 7.6 7.667

Carbon Monoxide & Nitrogen, % 80.9 81 80.8 80.900

Fuel Factor 1.16 1.17 1.15

Dry Molecular Weight, lb/lb-Mole 30.12 30.13 30.16 30.137

Wet Molecular weight, lb/lb-Mole 29.28 29.36 29.30 29.313

Flue Gas Static Pressure, inches of H2O -0.2 -0.2 -0.2 -0.200

Absolute Flue Gas Pressure, inches of Mercury 29.59 29.59 29.59 29.590

Average Stack Gas Temperature, °F 303.10 304.63 303.63 303.787

Average Velocity Head, inches of H2O 0.6154160230

65304

0.578491417

810915

0.635771952

895306

0.610

Average Stack Gas Velocity, feet/second 52.87 51.24 53.74 52.617

Stack Cross-Sectional Area, square feet 143.139 143.139 143.139 143.139

Dry Volumetric Flow Rate, dry scfm 289,146.2 281,414.0 293,195.2 287,918.467

Actual Wet Volumetric Flue Gas Flow Rate, acfm 454,065.5 440,066.5 461,537.4 451,889.800

Percent Isokinetic of Sampling Rate, % 98.5 98.8 98.6 98.633

Percent Excess Air, % 57.5 55.1 55.3 55.967

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

Round Duct Diameter, inches 162 162 162

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 09, 2011 Page 16 of 19
Location Stack - Method 3A CO2

Average

Run Number 1 2 3

Test Date 3/3/2010 3/3/2010 3/3/2010

Run Start Time 10:00:00 AM 1:39:00 PM 4:50:00 PM

Run Finish Time 12:28:00 PM 3:56:00 PM 7:04:00 PM

Carbon Dioxide, % 11.9 11.9 12 11.933

Oxygen, % 7.4 7.4 7.4 7.400

Fuel Factor 1.13 1.13 1.13

Dry Volumetric Flow Rate, dry scfm 279999 282242 286442 282,894.333

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

Moisture, % 6.3 6.3 6 6.200

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 20.1 20.1 20.1 20.100

Operating Units % % %

No. Readings/Avg.

Calibration Set 1 1 1 1.000

Calibration Pre Zero Cylinder ID XC011677B XC011677B XC011677B

Calibration Pre Zero Cylinder Instrument Response 0 0.1 0 0.033

Calibration Pre Zero Cylinder Bias 0 0.5 0 0.167

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC261893 CC261893 CC261893

Calibration Pre High Cylinder Instrument Response 10.1 10.1 10.1 10.100

Calibration Pre High Cylinder Bias -0.5 -0.5 -0.5 -0.500

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID XC011677B XC011677B XC011677B

Calibration Post Zero Cylinder Instrument Response 0 0 0.1 0.033

Calibration Post Zero Cylinder Bias 0 0 0.5 0.167

Calibration Post Zero Cylinder Drift 0 0.5 0.5 0.333

Calibration Post High Cylinder ID CC261893 CC261893 CC261893

Calibration Post High Cylinder Instrument Response 10.1 10.1 10 10.067

Calibration Post High Cylinder Bias -0.5 -0.5 -1 -0.667

Calibration Post High Cylinder Drift 0 0 0.5 0.167

Cavg 11.7 11.8 11.8 11.767

Cavg Units ppmvd ppmvd ppmvd

Cgas 11.8158 11.9254 11.985 11.909

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units ppmvw

Wednesday, February 09, 2011 Page 17 of 19
Location Stack - Method 3A O2

Average

Run Number 1 2 3

Test Date 3/3/2010 3/3/2010 3/3/2010

Run Start Time 10:00:00 AM 1:39:00 PM 4:50:00 PM

Run Finish Time 12:28:00 PM 3:56:00 PM 7:04:00 PM

Carbon Dioxide, % 11.9 11.9 12 11.933

Oxygen, % 7.4 7.4 7.4 7.400

Fuel Factor 1.13 1.13 1.13

Dry Volumetric Flow Rate, dry scfm 279999 282242 286442 282,894.333

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

Moisture, % 6.3 6.3 6 6.200

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 20.1 20.1 20.1 20.100

Operating Units % % %

No. Readings/Avg.

Calibration Set 2 2 2 2.000

Calibration Pre Zero Cylinder ID XC011677B XC011677B XC011677B

Calibration Pre Zero Cylinder Instrument Response 0.1 0.1 0 0.067

Calibration Pre Zero Cylinder Bias 0.5 0.5 0 0.333

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC261893 O2 CC261893 

O2

CC261893 

O2

Calibration Pre High Cylinder Instrument Response 10.1 10.1 10.1 10.100

Calibration Pre High Cylinder Bias 0 0 0 0.000

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID XC011677B XC011677B XC011677B

Calibration Post Zero Cylinder Instrument Response 0.1 0 0.1 0.067

Calibration Post Zero Cylinder Bias 0.5 0 0.5 0.333

Calibration Post Zero Cylinder Drift 0 0.5 0.5 0.333

Calibration Post High Cylinder ID CC261893 O2 CC261893 

O2

CC261893 

O2

Calibration Post High Cylinder Instrument Response 10.1 10.1 10.1 10.100

Calibration Post High Cylinder Bias 0 0 0 0.000

Calibration Post High Cylinder Drift 0 0 0 0.000

Cavg 7.4 7.3 7.4 7.367

Cavg Units ppmvd ppmvd ppmvd

Cgas 7.373 7.2861 7.3866 7.349

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Wednesday, February 09, 2011 Page 18 of 19
Location Stack - OTM - 27/28

Average

Run Number 1 2 3

Test Date 3/9/2010 3/9/2010 3/10/2010

Run Start Time 7:51:00 AM 2:31:00 PM 7:45:00 AM

Run Finish Time 2:00:00 PM 8:52:00 PM 2:06:00 PM

Net Traversing Points 78 75 78

Net Run Time, minutes 336.3 349.75 364

Nozzle Diameter, inches 0.185 0.185 0.185 0.185

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.981 0.981 0.981 0.981

Barometric Pressure, inches of Mercury 29.6 29.6 29.6 29.600

Average Orifice Meter Differential, inches H2O 0.49 0.50 0.49 0.493

Dry Gas Meter Volume Sampled, cubic feet 127.346 133.941 138.544 133.277

Average Dry Gas Meter Temperature, °F 84.54 83.33 85.40 84.423

Dry Gas Meter Volume Sampled, dscf 119.982 126.480 130.327 125.596

Total Moisture Liquid collected, g 172.8 163.5 210 182.100

Volume of Water Vapor, standard cubic feet 8.13 7.70 9.88 8.570

Moisture Content of Stack Gas, % 6.35 5.74 7.05 6.380

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

Dry Mole Fraction 0.9365 0.9426 0.9295 0.936

Carbon Dioxide, % 11.3 11.4 11.6 11.433

Oxygen, % 7.8 7.6 7.6 7.667

Carbon Monoxide & Nitrogen, % 80.9 81 80.8 80.900

Fuel Factor 1.16 1.17 1.15

Dry Molecular Weight, lb/lb-Mole 30.12 30.13 30.16 30.137

Wet Molecular weight, lb/lb-Mole 29.35 29.43 29.30 29.360

Flue Gas Static Pressure, inches of H2O -0.2 -0.2 -0.2 -0.200

Absolute Flue Gas Pressure, inches of Mercury 29.59 29.59 29.59 29.590

Average Stack Gas Temperature, °F 300.49 302.89 301.74 301.707

Average Velocity Head, inches of H2O 0.6325476250

33308

0.615883960

396563

0.646856563

632386

0.632

Average Stack Gas Velocity, feet/second 53.45 52.75 54.14 53.447

Stack Cross-Sectional Area, square feet 143.139 143.139 143.139 143.139

Dry Volumetric Flow Rate, dry scfm 295,181.1 292,290.4 296,269.8 294,580.433

Actual Wet Volumetric Flue Gas Flow Rate, acfm 459,046.8 453,034.9 464,972.7 459,018.133

Percent Isokinetic of Sampling Rate, % 92.7 94.9 92.7 93.433

Percent Excess Air, % 57.5 55.1 55.3 55.967

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

Round Duct Diameter, inches 162 162 162

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 09, 2011 Page 19 of 19