Name: Glenn Brannen

Title: Performance Group

Company: South Carolina Electric & Gas

Sign Date: 7/5/2010

Name: Mark Looney

Title: President

Company: Environmental Source Samplers, Inc

Sign Date: 7/5/2010

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.

Saturday, February 12, 2011 Page 1 of 15
7/5/2010

Facility Information:

Canadys Steam

CANADAYS STATION HIGHWAY 61

Canadys SC 29433

Contact: Glenn Brannen

Phone: 803-217-9690

Fax: 803-727-5155

Email: gbrannen@scana.com

Testing Company:

Environmental Source Samplers, Inc

436 Raleigh Street

Wilmington NC 28412

Contact:Mark Looney

Phone: 910-799-1055

Fax: 910-799-1056

Email: mark@essknowsair.com

Air Permit Number: Permitted Source ID/Name:

CAN3

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:

Canadys Generating Station consists of three (3) pulverized coal fired boilers. Unit 3 is a Foster Wheeler 

Corporation pulverized coal, tangentially fired, once-through, subcritical, reheat steam generator, with a turbinet rated 

at 127 MW. 

A baghouse has been added to this unit to remove particulate matter. 

A CEMS exists at the stack sampling location. The unit is designed to monitor SO2 (wet PPM), NOx (wet PPM), 

and CO2 (wet %). A NOX lb/MMBTU calculation is performed by the CEMS software, using CO2 as the diluent.

Industry/SCC/NAIS

Sampling Location Information:

Test Parameter Information:

AFS #: FRS #:

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

CAN3 192 0 0 0 366 1533 4 3

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

CAN3 Carbon Monoxide Method 10 3 240 0

CAN3 Total Particulate OTM - 27/28 3 240 0

CAN3 Filterable Particulate OTM - 27/28 3 240 0

Saturday, February 12, 2011 Page 2 of 15
7/5/2010

The following describes any modifications and/or deviations to the applicable test 

methods. If alternative methods were requested, see the attachments for documentation 

of request AND approval, including dates.

No Modification

CAN3 Filterable PM2.5 - PM10 OTM - 27/28 3 240 0

CAN3 Total PM2.5 OTM - 27/28 3 240 0

Organic Condensible 

Particulate

CAN3 OTM - 27/28 3 240 0

Inorganic (Aqueous) 

Condensible Part.

CAN3 OTM - 27/28 3 240 0

CAN3 Filterable PM2.5 OTM - 27/28 3 240 0

CAN3 Lead Method 29 3 240 0

CAN3 Selenium Method 29 3 240 0

CAN3 Nickel Method 29 3 240 0

CAN3 Manganese Method 29 3 240 0

CAN3 Antimony Method 29 3 240 0

CAN3 Arsenic Method 29 3 240 0

CAN3 Cobalt Method 29 3 240 0

CAN3 Cadmium Method 29 3 240 0

CAN3 Beryllium Method 29 3 240 0

CAN3 Chromium Method 29 3 240 0

CAN3 Mercury Method 29 3 240 0

CAN3 Co2 Method 3A CO2 3 240 0

CAN3 O2 Method 3A O2 3 240 0

Saturday, February 12, 2011 Page 3 of 15
7/5/2010

Sampling / Stack Data Results Summary

Location CAN3 - 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 92.339 91.22 92.893 92.151

Moisture, %

Fuel Type CC41265 CC41265 CC41265

Fw 0.32 -0.9 0.92 0.113

Fc 0 0 0 0.000

Location CAN3 - Method 29

Average

Run Number 1 2 3

Test Date 5/12/2010 5/13/2010 5/13/2010

Run Start Time 4:04:00 PM 11:15:00 

AM

6:00:00 PM

Run Finish Time 8:30:00 PM 3:46:00 PM 10:24:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 161.971 163.780 160.158 161.970

Moisture Content of Stack Gas, % 7.12 7.18 7.21 7.170

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

Carbon Dioxide, % 11.977 11.841 11.685 11.834

Oxygen, % 7.7192 7.8108 7.9209 7.817

Average Stack Gas Temperature, °F 283.98 295.00 295.00 291.327

Dry Volumetric Flow Rate, dry scfm 516,093.1 513,588.0 513,887.6 514,522.900

Actual Wet Volumetric Flue Gas Flow Rate, acfm 789,811.7 798,135.7 798,859.5 795,602.300

Percent Isokinetic of Sampling Rate, % 107.3 109.0 106.5 107.600

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

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Saturday, February 12, 2011 Page 4 of 15
7/5/2010

Location CAN3 - Method 3A CO2

Average

Run Number 1 2 3

Test Date 5/12/2010 5/13/2010 5/13/2010

Run Start Time 4:05:00 PM 11:15:00 

AM

6:00:00 PM

Run Finish Time 8:04:00 PM 3:14:00 PM 9:59:00 PM

Carbon Dioxide, % 11.977 11.841 11.685 11.834

Oxygen, % 7.7192 7.8108 7.9209 7.817

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 7.12 7.18 7.21 7.170

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location CAN3 - Method 3A O2

Average

Run Number 1 2 3

Test Date 5/12/2010 5/13/2010 5/13/2010

Run Start Time 4:05:00 PM 11:15:00 

AM

6:00:00 PM

Run Finish Time 8:04:00 PM 3:14:00 PM 9:59:00 PM

Carbon Dioxide, % 11.977 11.841 11.685 11.834

Oxygen, % 7.7192 7.8108 7.9209 7.817

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 7.12 7.18 7.21 7.170

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Saturday, February 12, 2011 Page 5 of 15
7/5/2010

Location CAN3 - OTM - 27/28

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

Saturday, February 12, 2011 Page 6 of 15
7/5/2010

Emissions Summary

Location: CAN3 - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

ppm 8.73E+01 8.19E+01 7.19E+01 80.367

ppm@7%O2 9.21E+01 8.70E+01 7.70E+01 85.367

Location: CAN3 - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.00555 0.0026965 0.002496 0.004

lb/mmBtuO2 1.17E-06 5.67E-07 5.41E-07 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.01646 0.019815 0.0217 0.019

lb/mmBtuO2 3.47E-06 4.17E-06 4.70E-06 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.000675 0.001075 0.001255 0.001

lb/mmBtuO2 1.42E-07 2.26E-07 2.72E-07 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.00438 0.0009565 0.000948 0.002

lb/mmBtuO2 9.25E-07 2.01E-07 2.06E-07 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.01367 0.01795 0.02241 0.018

lb/mmBtuO2 2.89E-06 3.77E-06 4.86E-06 0.000

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.00685 0.005043 0.0045 0.005

lb/mmBtuO2 1.45E-06 1.06E-06 9.76E-07 0.000

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.006419 0.010091 0.013279 0.010

lb/mmBtuO2 1.35E-06 2.12E-06 2.88E-06 0.000

Saturday, February 12, 2011 Page 7 of 15
7/5/2010

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.0543 0.027005 0.01829 0.033

lb/mmBtuO2 1.15E-05 5.68E-06 3.96E-06 0.000

Compound: Mercury

Average

RunNumber 1 2 3

Mass_mg 0.00007 0.000255 0.000285 0.000

lb/mmBtuO2 1.48E-08 5.36E-08 6.18E-08 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.19907 0.039655 0.01826 0.086

lb/mmBtuO2 4.20E-05 8.34E-06 3.96E-06 0.000

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.04 0.054125 0.06714 0.054

lb/mmBtuO2 8.44E-06 1.14E-05 1.46E-05 0.000

Location: CAN3 - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 8.4 58.1 41.1 35.867

lb/mmBtuO2 3.32E-03 2.25E-02 1.62E-02 0.014

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 1.5 10.9 6.9 6.433

lb/mmBtuO2 5.92E-04 4.22E-03 2.72E-03 0.003

Compound: Filterable PM2.5 - PM10

Average

RunNumber 1 2 3

Mass_mg 3.6 34.6 25.2 21.133

lb/mmBtuO2 1.42E-03 1.34E-02 9.94E-03 0.008

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 21.9 15.8 26.3 21.333

lb/mmBtuO2 8.65E-03 6.12E-03 1.04E-02 0.008

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 17.5 2.8 5.3 8.533

Saturday, February 12, 2011 Page 8 of 15
7/5/2010

Process Run Data

lb/mmBtuO2 6.91E-03 1.08E-03 2.09E-03 0.003

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 47.8 76.7 72.7 65.733

lb/mmBtuO2 1.89E-02 2.97E-02 2.87E-02 0.026

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 40.9 29.5 38.5 36.300

lb/mmBtuO2 1.62E-02 1.14E-02 1.52E-02 0.014

Saturday, February 12, 2011 Page 9 of 15
7/5/2010

Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input Million Btus/million BTU using O2 1746.2 0

2 Heat Input Million Btus/million BTU using O2 1797.6 0

3 Heat Input Million Btus/million BTU using O2 1768.8 0

1 0 0

2 0 0

3 0 0

1 Stack Flow 497 KSCFM 0

2 Stack Flow 508 KSCFM 0

3 Stack Flow 507 KSCFM 0

1 Unit Gross Electrical Output 190.64 MW 0

2 Unit Gross Electrical Output 194.71 MW 0

3 Unit Gross Electrical Output 195.54 MW 0

Run Name Value UOM Comments

Target

Value

1 BAGHOUSE 0 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value 0 Btu/b

1 Fuel Moisture 0 %

1 Fuel Mercury Content 0 ppm

1 Fuel Cadmium Content 0 ppm

1 Ultimate/Proximate Analysis 0

1 Fuel Nickel Content 0 ppm

1 Fuel Arsenic Content 0 ppm

1 Fuel Chromium Content 0 ppm

1 Fuel Beryllium Content 0 ppm

1 Fuel Lead Content 0 ppm

1 Fuel Manganese Content 0 ppm

1 Fuel Chlorine Content 0 ppm

1 Fuel Fluorine Content 0 ppm

Saturday, February 12, 2011 Page 10 of 15
7/5/2010

Sampling / Stack Data Results Detail

Location CAN3 - Method 10

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor 475042 475042 475042

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2 92.339 91.22 92.893 92.151

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number CAN3 CAN3 CAN3

Operating Range Method 10 Method 10 Method 10

Operating Units 1 2 3

No. Readings/Avg. 5/12/2010 5/13/2010 5/13/2010

Calibration Set 8:04:00 PM 3:14:00 PM 9:59:00 PM

Calibration Pre Zero Cylinder ID 0 0 0

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias 7.12 7.18 7.21 7.170

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID 11.977 11.841 11.685

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias 7.7192 7.8108 7.9209 7.817

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 0 0 0 0.000

Calibration Post High Cylinder ID % % %

Calibration Post High Cylinder Instrument Response 240 240 240 240.000

Calibration Post High Cylinder Bias 1 1 1 1.000

Calibration Post High Cylinder Drift 3 3 3 3.000

Cavg 475042 475042 475042 475,042.000

Cavg Units 0.755 1.11 1.433

Cgas 2.02 2.4 2.75 2.390

Cgas Units 0 0 0

Fuel Type CC41265 CC41265 CC41265

Fw 0.32 -0.9 0.92 0.113

Fc 0 0 0 0.000

Cgasw 1.11 1.433 1.433 1.325

Cgasw Units 2.4 2.75 2.75

Saturday, February 12, 2011 Page 11 of 15
7/5/2010

Location CAN3 - Method 29

Average

Run Number 1 2 3

Test Date 5/12/2010 5/13/2010 5/13/2010

Run Start Time 4:04:00 PM 11:15:00 AM 6:00:00 PM

Run Finish Time 8:30:00 PM 3:46:00 PM 10:24:00 PM

Net Traversing Points 1 1 1

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.212 0.212 0.212 0.212

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9986 0.9986 0.9986 0.999

Barometric Pressure, inches of Mercury 29.71 29.71 29.71 29.710

Average Orifice Meter Differential, inches H2O 1.48 1.24 1.48 1.400

Dry Gas Meter Volume Sampled, cubic feet 172.008 172.838 169.689 171.512

Average Dry Gas Meter Temperature, °F 98.04 94.21 96.75 96.333

Dry Gas Meter Volume Sampled, dscf 161.971 163.780 160.158 161.970

Total Moisture Liquid collected, g 263.6 269.1 264.5 265.733

Volume of Water Vapor, standard cubic feet 12.41 12.67 12.45 12.510

Moisture Content of Stack Gas, % 7.12 7.18 7.21 7.170

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

Dry Mole Fraction 0.9288 0.9282 0.9279 0.928

Carbon Dioxide, % 11.977 11.841 11.685 11.834

Oxygen, % 7.7192 7.8108 7.9209 7.817

Carbon Monoxide & Nitrogen, % 80.3038 80.3482 80.3941 80.349

Fuel Factor 1.10 1.11 1.11

Dry Molecular Weight, lb/lb-Mole 30.23 30.21 30.19 30.210

Wet Molecular weight, lb/lb-Mole 29.36 29.33 29.31 29.333

Flue Gas Static Pressure, inches of H2O -0.65 -0.65 -0.65 -0.650

Absolute Flue Gas Pressure, inches of Mercury 29.66 29.66 29.66 29.660

Average Stack Gas Temperature, °F 283.98 295.00 295.00 291.327

Average Velocity Head, inches of H2O 0.973 0.978 0.979 0.977

Average Stack Gas Velocity, feet/second 65.47 66.16 66.22 65.950

Stack Cross-Sectional Area, square feet 201.062 201.062 201.062 201.062

Dry Volumetric Flow Rate, dry scfm 516,093.1 513,588.0 513,887.6 514,522.900

Actual Wet Volumetric Flue Gas Flow Rate, acfm 789,811.7 798,135.7 798,859.5 795,602.300

Percent Isokinetic of Sampling Rate, % 107.3 109.0 106.5 107.600

Percent Excess Air, % 57.3 58.3 59.5 58.367

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

Round Duct Diameter, inches 192 192 192

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

Saturday, February 12, 2011 Page 12 of 15
7/5/2010

Location CAN3 - Method 3A CO2

Average

Run Number 1 2 3

Test Date 5/12/2010 5/13/2010 5/13/2010

Run Start Time 4:05:00 PM 11:15:00 AM 6:00:00 PM

Run Finish Time 8:04:00 PM 3:14:00 PM 9:59:00 PM

Carbon Dioxide, % 11.977 11.841 11.685 11.834

Oxygen, % 7.7192 7.8108 7.9209 7.817

Fuel Factor 1.1 1.11 1.11

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 7.12 7.18 7.21 7.170

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 0 0 0 0.000

Operating Units % % %

No. Readings/Avg. 240 240 240 240.000

Calibration Set 1 1 1 1.000

Calibration Pre Zero Cylinder ID 475042 475042 475042

Calibration Pre Zero Cylinder Instrument Response -0.035 -0.056 0.225 0.045

Calibration Pre Zero Cylinder Bias 0.13 0 1.75 0.627

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID XCO01052BCO2XCO01052B

-CO2

XCO01052BCO2

Calibration Pre High Cylinder Instrument Response 16.01 15.956 16.257 16.074

Calibration Pre High Cylinder Bias -0.58 -0.92 0.95 -0.183

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID 475042 475042 475042

Calibration Post Zero Cylinder Instrument Response -0.056 0.225 0.005 0.058

Calibration Post Zero Cylinder Bias 0 1.75 0.38 0.710

Calibration Post Zero Cylinder Drift 0.13 1.75 1.37 1.083

Calibration Post High Cylinder ID XCO01052BCO2XCO01052B

-CO2

XCO01052BCO2

Calibration Post High Cylinder Instrument Response 15.956 16.257 16.028 16.080

Calibration Post High Cylinder Bias -0.92 0.95 -0.47 -0.147

Calibration Post High Cylinder Drift 0.34 1.87 1.42 1.210

Cavg 11.893 11.883 11.762 11.846

Cavg Units %vd %vd %vd

Cgas 11.9769 11.8412 11.6852 11.834

Cgas Units %vd %vd %vd

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

Saturday, February 12, 2011 Page 13 of 15
7/5/2010

Location CAN3 - Method 3A O2

Average

Run Number 1 2 3

Test Date 5/12/2010 5/13/2010 5/13/2010

Run Start Time 4:05:00 PM 11:15:00 AM 6:00:00 PM

Run Finish Time 8:04:00 PM 3:14:00 PM 9:59:00 PM

Carbon Dioxide, % 11.977 11.841 11.685 11.834

Oxygen, % 7.7192 7.8108 7.9209 7.817

Fuel Factor 1.1 1.11 1.11

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 7.12 7.18 7.21 7.170

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 0 0 0 0.000

Operating Units % % %

No. Readings/Avg. 240 240 240 240.000

Calibration Set 2 2 2 2.000

Calibration Pre Zero Cylinder ID 475042 475042 475042

Calibration Pre Zero Cylinder Instrument Response 0.055 0.076 0.155 0.095

Calibration Pre Zero Cylinder Bias 0.46 0.64 1.3 0.800

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID XCO01052BO2XCO01052B

-O2

XCO01052BO2

Calibration Pre High Cylinder Instrument Response 11.933 11.995 12.103 12.010

Calibration Pre High Cylinder Bias 99.77 100.29 101.2 100.420

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID 475042 475042 475042

Calibration Post Zero Cylinder Instrument Response 0.076 0.155 0.077 0.103

Calibration Post Zero Cylinder Bias 0.64 1.3 0.64 0.860

Calibration Post Zero Cylinder Drift 0.18 0.66 0.66 0.500

Calibration Post High Cylinder ID XCO01052BO2XCO01052B

-O2

XCO01052BO2

Calibration Post High Cylinder Instrument Response 11.995 12.103 12.022 12.040

Calibration Post High Cylinder Bias 100.29 101.2 100.52 100.670

Calibration Post High Cylinder Drift 0.5200000000

0001

0.909999999

999997

0.680000000

000007

0.703

Cavg 7.745 7.909 8.028 7.894

Cavg Units %vd %vd %vd

Cgas 7.7192 7.8108 7.9209 7.817

Cgas Units %vd %vd %vd

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

Saturday, February 12, 2011 Page 14 of 15
7/5/2010

Location CAN3 - OTM - 27/28

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

Saturday, February 12, 2011 Page 15 of 15