### 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.

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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 192 366 1533 4 0 3 0 0

Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location 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 CAN3


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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.
No Modification

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

Particulate OTM - 27/28 3 240 0 CAN3
Inorganic (Aqueous)

Condensible Part. 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 CAN3



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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



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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



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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



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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



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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


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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



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Process Run Data

APCD Run Data

Process Lab Run Data 

### Run Name Value UOM Comments Target Value 1 Heat Input 1746.2 Million Btus/million BTU using O2 0


### 2 Heat Input 1797.6 Million Btus/million BTU using O2 0
3 Heat Input 1768.8 Million Btus/million BTU using O2 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



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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



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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



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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 XCO01052BCO2 XCO01052B

-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 XCO01052BCO2 XCO01052B

-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



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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 XCO01052BO2 XCO01052B

-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 XCO01052BO2 XCO01052B

-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



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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



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