Name: Glenn Brannen

Title: Preformance Group

Company: South Carolina Electric and Gas

Sign Date: 8/3/2010

Name: Mark Looney

Title: President

Company: Environmental Source Samplers, Inc

Sign Date: 8/3/2010

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 17
8/3/2010

Facility Information:

COPE

405 TEAMWORK DRIVE

Cope SC 29038

Contact: Glenn Brannen

Phone: 803-217-9690

Fax:

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:

COP1 COPE UNIT 1

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:

A primary and redundant CEMS exists at the stack sampling location. The unit is designed to monitor flowrate 

(WSCFM), 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. 

A solo CEMS exists for the SO2 and CO2 scrubber inlet measurements. Using time sharing, the single monitors are 

able to sample from both of the inlet ducts. The units are designed to sample from both of the inlet ducts. The units 

are designed to monitor SO2 (wet ppm) and CO2 (wet %). A SO2 lb/mmbtu calculation is performed by the CEMS 

software, using CO2 as the diluent. This lb/mmbtu calculation is also reported for the SO2 and CO2 measured by the 

Part 75 system in the stack.

Industry/SCC/NAIS

Sampling Location Information:

Test Parameter Information:

AFS #: FRS #:

SCC / Description 10100203 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Cyclone Furnace (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

COP1 288 0 0 0 2547.6 3174 4 3

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

COP1 Carbon Monoxide Method 10 3 180 0

Saturday, February 12, 2011 Page 2 of 17
8/3/2010

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

Total organic compounds 

(TOC) as Propane

COP1 Method 25A 3 180 0

Inorganic (Aqueous) 

Condensible Part.

COP1 OTM - 27/28 3 240 0

COP1 Filterable PM2.5 OTM - 27/28 3 240 0

COP1 Filterable PM2.5 - PM10 OTM - 27/28 3 240 0

COP1 Total PM2.5 OTM - 27/28 3 240 0

COP1 Filterable PM10 OTM - 27/28 3 240 0

COP1 Filterable Particulate OTM - 27/28 3 240 0

Organic Condensible 

Particulate

COP1 OTM - 27/28 3 240 0

COP1 Total Particulate OTM - 27/28 3 240 0

COP1 Manganese Method 29 3 240 0

COP1 Antimony Method 29 3 240 0

COP1 Beryllium Method 29 3 240 0

COP1 Cadmium Method 29 3 240 0

COP1 Chromium Method 29 3 240 0

COP1 Cobalt Method 29 3 240 0

COP1 Lead Method 29 3 240 0

COP1 Nickel Method 29 3 240 0

COP1 Selenium Method 29 3 240 0

COP1 Mercury Method 29 3 240 0

COP1 Arsenic Method 29 3 240 0

COP1 Co2 Method 3A CO2 3 180 0

COP1 O2 Method 3A O2 3 180 0

Saturday, February 12, 2011 Page 3 of 17
8/3/2010

Sampling / Stack Data Results Summary

Location COP1 - 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 COP1 - 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

Saturday, February 12, 2011 Page 4 of 17
8/3/2010

Location COP1 - Method 29

Average

Run Number 1 2 3

Test Date 6/8/2010 6/8/2010 6/8/2010

Run Start Time 9:50:00 AM 2:50:00 PM 12:15:00 AM

Run Finish Time 2:20:00 PM 7:15:00 PM 7:40:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 168.896 169.256 168.918 169.023

Moisture Content of Stack Gas, % 11.48 11.09 10.62 11.063

Moisture Saturation at Stack Gas Temperature, % 40.32 38.89 38.51 39.240

Carbon Dioxide, % 12.56 12.68 12.6 12.613

Oxygen, % 6.92 6.9 6.97 6.930

Average Stack Gas Temperature, °F 169.52 167.94 167.52 168.327

Dry Volumetric Flow Rate, dry scfm 955,123.4 960,815.8 964,912.2 960,283.800

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,289,037.2 1,288,222.9 1,286,051.4 1,287,770.50

0

Percent Isokinetic of Sampling Rate, % 97.0 96.6 96.0 96.533

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 COP1 - 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

Saturday, February 12, 2011 Page 5 of 17
8/3/2010

Location COP1 - 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 COP1 - 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 17
8/3/2010

Emissions Summary

Location: COP1 - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 1.30E-02 6.31E-03 3.50E-03 0.008

ppm 1.23E+01 5.95E+00 3.28E+00 7.177

ppm@7%O2 1.22E+01 5.91E+00 3.27E+00 7.127

Location: COP1 - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 1.21E-03 3.26E-02 3.87E-03 0.013

ppm 7.20E-01 1.95E+01 2.31E+00 7.510

ppm@7%O2 7.16E-01 1.94E+01 2.31E+00 7.475

Location: COP1 - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.000889 0.0013605 0.000351 0.001

lb/mmBtuO2 1.70E-07 2.59E-07 6.72E-08 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.000731 0.000531 0.000523 0.001

lb/mmBtuO2 1.40E-07 1.01E-07 1.00E-07 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.000084 0.00005 0.00005 0.000

lb/mmBtuO2 1.60E-08 9.51E-09 9.58E-09 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.000332 0.0002745 0.00024 0.000

lb/mmBtuO2 6.34E-08 5.22E-08 4.60E-08 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.00549 0.003321 0.00411 0.004

lb/mmBtuO2 1.05E-06 6.32E-07 7.87E-07 0.000

Compound: Cobalt

Average

RunNumber 1 2 3

Saturday, February 12, 2011 Page 7 of 17
8/3/2010

Mass_mg 0.000459 0.000548 0.000206 0.000

lb/mmBtuO2 8.76E-08 1.04E-07 3.95E-08 0.000

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.001143 0.000904 0.001611 0.001

lb/mmBtuO2 2.18E-07 1.72E-07 3.09E-07 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.0237 0.32257 0.02835 0.125

lb/mmBtuO2 4.52E-06 6.13E-05 5.43E-06 0.000

Compound: Mercury

Average

RunNumber 1 2 3

Mass_mg 0.000078 0.000917 0.000116 0.000

lb/mmBtuO2 1.49E-08 1.74E-07 2.22E-08 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.0062 0.002835 0.00318 0.004

lb/mmBtuO2 1.18E-06 5.39E-07 6.09E-07 0.000

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.000657 0.0006 0.0006 0.001

lb/mmBtuO2 1.25E-07 1.14E-07 1.15E-07 0.000

Location: COP1 - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 6.3 14.2 6.2 8.900

lb/mmBtuO2 2.57E-03 5.79E-03 2.49E-03 0.004

Compound: Filterable PM10

Average

RunNumber 1 2 3

Mass_mg 1.5 1.3 2 1.600

lb/mmBtuO2 6.11E-04 5.30E-04 8.02E-04 0.001

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 1.1 2.5 4.1 2.567

lb/mmBtuO2 4.48E-04 1.02E-03 1.65E-03 0.001

Saturday, February 12, 2011 Page 8 of 17
8/3/2010

Process Run Data

Compound: Filterable PM2.5 - PM10

Average

RunNumber 1 2 3

Mass_mg 3.8 10.5 0.2 4.833

lb/mmBtuO2 1.55E-03 4.28E-03 8.02E-05 0.002

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 46.8 47.8 49 47.867

lb/mmBtuO2 1.91E-02 1.95E-02 1.97E-02 0.019

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 27.6 28.8 9.8 22.067

lb/mmBtuO2 1.12E-02 1.17E-02 3.93E-03 0.009

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 80.7 90.8 65 78.833

lb/mmBtuO2 3.29E-02 3.70E-02 2.61E-02 0.032

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 75.5 79.1 62.9 72.500

lb/mmBtuO2 3.08E-02 3.23E-02 2.52E-02 0.029

Saturday, February 12, 2011 Page 9 of 17
8/3/2010

Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Average Heat Input 3372.8 MMBtu/hr M29/OTM27%28/

M3A/M10/M316/

M26 Run 1 

6/8/201 09:50 - 

14:20

0

2 Average Heat Input 3357.9 MMBtu/hr M29/OTM27%28/

M3A/M10/M316/

M26 Run 2 

6/8/2010 14:50 - 

19:15

0

3 Average Heat Input 3229.6 MMBtu/hr M29/OTM27%28/

M3A/M10/M316/

M26 Run 1 

6/8/201 19:40 - 

00:15

0

1 Unit Gross Electical Output 396.1 MW M29/OTM27%28/

M3A/M10/M316/

M26 Run 1 

6/8/2010 09:50 - 

14:20

0

2 Unit Gross Electical Output 396.1 MW M29/OTM27%28/

M3A/M10/M316/

M26 Run 2 

6/8/2010 14:50 - 

19:15

0

3 Unit Gross Electical Output 378.7 MW M29/OTM27%28/

M3A/M10/M316/

M26 Run 1 

6/8/201 19:40 - 

00:15

0

Run Name Value UOM Comments

Target

Value

1 BAGHOUSE 0 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value 12689 Btu/lb

2 Fuel Higher Heating Value 12216 Btu/lb

3 Fuel Higher Heating Value 12707 Btu/lb

1 Fuel Moisture 4.518 %

2 Fuel Moisture 6.161 %

3 Fuel Moisture 4.391 %

Saturday, February 12, 2011 Page 10 of 17
8/3/2010

1 Fuel Mercury Content 0.08 ug/g

2 Fuel Mercury Content 0.08 ug/g

3 Fuel Mercury Content 0.07 ug/g

1 Fuel Cadmium Content 0.2 ug/g

2 Fuel Cadmium Content 0.2 ug/g

3 Fuel Cadmium Content 0.2 ug/g

1 Fuel Nickel Content 14 ug/g

2 Fuel Nickel Content 15 ug/g

3 Fuel Nickel Content 13 ug/g

1 Fuel Arsenic Content 5 ug/g

2 Fuel Arsenic Content 4 ug/g

3 Fuel Arsenic Content 5 ug/g

1 Fuel Chromium Content 19 ug/g

2 Fuel Chromium Content 21 ug/g

3 Fuel Chromium Content 16 ug/g

1 Fuel Beryllium Content 2.2 ug/g

2 Fuel Beryllium Content 2.3 ug/g

3 Fuel Beryllium Content 1.9 ug/g

1 Fuel Lead Content 7 ug/g

2 Fuel Lead Content 8 ug/g

3 Fuel Lead Content 6 ug/g

1 Fuel Manganese Content 12 ug/g

2 Fuel Manganese Content 12 ug/g

3 Fuel Manganese Content 13 ug/g

1 Fuel Chlorine Content 960 ug/g

2 Fuel Chlorine Content 930 ug/g

3 Fuel Chlorine Content 720 ug/g

1 Fuel Fluorine Content 79 ug/g

2 Fuel Fluorine Content 75 ug/g

3 Fuel Fluorine Content 69 ug/g

Saturday, February 12, 2011 Page 11 of 17
8/3/2010

Sampling / Stack Data Results Detail

Location COP1 - 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

Saturday, February 12, 2011 Page 12 of 17
8/3/2010

Location COP1 - 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

Saturday, February 12, 2011 Page 13 of 17
8/3/2010

Location COP1 - Method 29

Average

Run Number 1 2 3

Test Date 6/8/2010 6/8/2010 6/8/2010

Run Start Time 9:50:00 AM 2:50:00 PM 12:15:00 AM

Run Finish Time 2:20:00 PM 7:15:00 PM 7:40:00 PM

Net Traversing Points 1 1 1

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.251 0.251 0.251 0.251

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.0001 1.0001 1.0001 1.000

Barometric Pressure, inches of Mercury 29.9 29.9 29.9 29.900

Average Orifice Meter Differential, inches H2O 1.72 1.72 1.72 1.720

Dry Gas Meter Volume Sampled, cubic feet 178.775 182.015 178.933 179.908

Average Dry Gas Meter Temperature, °F 100.93 109.88 101.35 104.053

Dry Gas Meter Volume Sampled, dscf 168.896 169.256 168.918 169.023

Total Moisture Liquid collected, g 465.3 448.5 426.6 446.800

Volume of Water Vapor, standard cubic feet 21.90 21.11 20.08 21.030

Moisture Content of Stack Gas, % 11.48 11.09 10.62 11.063

Moisture Saturation at Stack Gas Temperature, % 40.32 38.89 38.51 39.240

Dry Mole Fraction 0.8852 0.8891 0.8938 0.889

Carbon Dioxide, % 12.56 12.68 12.6 12.613

Oxygen, % 6.92 6.9 6.97 6.930

Carbon Monoxide & Nitrogen, % 80.52 80.42 80.43 80.457

Fuel Factor 1.11 1.10 1.11

Dry Molecular Weight, lb/lb-Mole 30.29 30.30 30.29 30.293

Wet Molecular weight, lb/lb-Mole 28.88 28.94 28.98 28.933

Flue Gas Static Pressure, inches of H2O -0.61 -0.62 -0.62 -0.617

Absolute Flue Gas Pressure, inches of Mercury 29.86 29.85 29.85 29.853

Average Stack Gas Temperature, °F 169.52 167.94 167.52 168.327

Average Velocity Head, inches of H2O 0.599 0.601 0.6 0.600

Average Stack Gas Velocity, feet/second 47.49 47.46 47.38 47.443

Stack Cross-Sectional Area, square feet 452.389 452.389 452.389 452.389

Dry Volumetric Flow Rate, dry scfm 955,123.4 960,815.8 964,912.2 960,283.800

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,289,037.2 1,288,222.9 1,286,051.4 1,287,770.5

00

Percent Isokinetic of Sampling Rate, % 97.0 96.6 96.0 96.533

Percent Excess Air, % 48.3 48.1 48.9 48.433

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

Round Duct Diameter, inches 288 288 288

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 14 of 17
8/3/2010

Location COP1 - 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

Saturday, February 12, 2011 Page 15 of 17
8/3/2010

Location COP1 - 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

Saturday, February 12, 2011 Page 16 of 17
8/3/2010

Location COP1 - 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 17 of 17