Name: Richard Ramsdell

Title: Plant Manager

Company: Ebensburg Power Company

Sign Date: 9/2/2010

Name: Stephen Schell

Title: President

Company: Air Analysis, LLC

Sign Date: 9/2/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Ebensburg Power - ICR

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.

Thursday, January 20, 2011 Page 1 of 17
Ebensburg Power - ICR

9/2/2010

Facility Information:

Ebensburg Power

P.O. Box 845

Ebensburg PA 15931

Contact: Richard Ramsdell

Phone: 814 472-1140 ext 305

Fax: 814 472-1143

Email: RRamsdell@ebensburgpower.com

Testing Company:

Air Analysis, LLC t/a SGF Consulting Services

189 Hausman Road

Lenhartsville PA 19534

Contact: Stephen Schell

Phone: 610 756-3490

Fax: 610 756-3491

Email: sschell@hughes.net

Air Permit Number:

11-00318

Permitted Source ID/Name:

031 Ebensburg Power

Permitted Maximum Process Rate: Max. Normal Operation Process Rate:

510 klbs/hr Steam Flow

Target Process Test Rate

90% of Maximum Load

Description of the source (including control equipment). Please see the attachments for source or

 process flow diagram:

The Ebensburg Power Company is located in Ebensburg, Cambria County, Pennsylvania. A circulating fluidized bed 

boiler is the primary steam generating unit within the Ebensburg Power facility. The CFB boiler burns bituminous 

waste coal and operates on a continuous basis. The CFB boiler as a current capacity to produce 510 klbs/hr of steam 

at 1,500 psig at 955 degrees F. The CFB boiler is equipped with a limestone addition feature for sulfur dioxide 

emissions control and a baghouse for particulate emissions control. Flue gas emissions are discharged through the 

baghouse to the atmosphere by a vertical stack.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 420210067 FRS #: 110000330632

SCC / Description 10102018 External Combustion Boilers - Electric Generation - Waste Coal - Circulating 

Fluidized Bed Combustion 

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 105 0 0 105 1338 1662 2 6

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack % H2O Method 1 - 4 0 During each test run

Flowrate Method 1 - 4 0 Throughout testing 

program

Stack

Stack Carbon Monoxide Method 10 3 120 0

Thursday, January 20, 2011 Page 2 of 17
Ebensburg Power - ICR

9/2/2010

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.

Custom Method 0010 3 120 0 Speciated Semi VOC 

HAPS

Stack

Stack Formaldehyde Method 0011 3 120 0

Stack Custom Method 18 3 120 0 Methane

Total organic compounds 

(TOC) as Propane

Stack Method 25A 3 120 0

Stack Filterable Particulate OTM - 27/28 3 330 0

Stack Total PM2.5 OTM - 27/28 3 330 0

Stack Total Particulate OTM - 27/28 3 330 0

Stack Filterable PM2.5 OTM - 27/28 3 330 0

Stack Manganese Method 29 3 240 0

Stack Filterable Particulate Method 29 3 240 0

Stack Antimony Method 29 3 240 0

Stack Arsenic Method 29 3 240 0

Stack Beryllium Method 29 3 240 0

Stack Cadmium Method 29 3 240 0

Stack Chromium Method 29 3 240 0

Stack Selenium Method 29 3 240 0

Stack Lead Method 29 3 240 0

Stack Nickel Method 29 3 240 0

Stack Cobalt Method 29 3 240 0

Stack Co2 Method 3A CO2 0 During each test run

Stack O2 Method 3A O2 0 During each test run

Stack Mercury Method 30B 3 120 0

Stack Custom Method 0031 3 120 0 Speciated VOC HAPS

Stack Sulfur Dioxide Method 6C 3 120 0

Thursday, January 20, 2011 Page 3 of 17
Ebensburg Power - ICR

9/2/2010

Sampling / Stack Data Results Summary

Location Stack - 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 - 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

Thursday, January 20, 2011 Page 4 of 17
Ebensburg Power - ICR

9/2/2010

Location Stack - Method 29

Average

Run Number 1 2 3

Test Date 7/26/2010 7/28/2010 7/29/2010

Run Start Time 1:10:00 PM 7:35:00 

AM

6:10:00 AM

Run Finish Time 7:15:00 PM 1:44:00 PM 12:07:00 PM

Net Run Time, minutes 330 330 330

Dry Gas Meter Volume Sampled, dscf 259.084 257.827 260.227 259.046

Moisture Content of Stack Gas, % 8.40 9.11 9.61 9.040

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

Carbon Dioxide, % 15.49 15.77 15.95 15.737

Oxygen, % 4.06 3.74 3.71 3.837

Average Stack Gas Temperature, °F 328.42 328.25 328.00 328.223

Dry Volumetric Flow Rate, dry scfm 166,332.4 163,044.6 163,680.1 164,352.367

Actual Wet Volumetric Flue Gas Flow Rate, acfm 269,078.7 266,913.9 270,161.0 268,717.867

Percent Isokinetic of Sampling Rate, % 104.6 106.2 106.8 105.867

F-Factor, dscfm/MMBtu @ %O2 10041 10007 10165 10,071.000

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Stack - 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

Thursday, January 20, 2011 Page 5 of 17
Ebensburg Power - ICR

9/2/2010

Location Stack - 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

Thursday, January 20, 2011 Page 6 of 17
Ebensburg Power - ICR

9/2/2010

Emissions Summary

Location: Stack - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 1.47E-01 1.66E-01 1.57E-01 0.157

ppm 1.60E+02 1.79E+02 1.54E+02 164.333

ppm@7%O2 1.33E+02 1.49E+02 1.30E+02 137.333

Location: Stack - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 1.10E-03 1.29E-03 1.59E-06 0.001

ppm 7.60E-01 8.86E-01 9.88E-04 0.549

ppm@7%O2 6.31E-01 7.39E-01 8.33E-04 0.457

Location: Stack - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.004 0.004 0.004 0.004

lb/mmBtuO2 4.24E-07 4.17E-07 4.19E-07 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.0445 0.029 0.0268 0.033

lb/mmBtuO2 4.72E-06 3.02E-06 2.81E-06 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.00142 0.00106 0.001 0.001

lb/mmBtuO2 1.51E-07 1.10E-07 1.05E-07 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.00323 0.00935 0.00779 0.007

lb/mmBtuO2 3.43E-07 9.74E-07 8.16E-07 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.0295 0.0248 0.0224 0.026

lb/mmBtuO2 3.13E-06 2.58E-06 2.35E-06 0.000

Compound: Cobalt

Average

RunNumber 1 2 3

Thursday, January 20, 2011 Page 7 of 17
Ebensburg Power - ICR

9/2/2010

Mass_mg 0.00563 0.00436 0.00376 0.005

lb/mmBtuO2 5.97E-07 4.54E-07 3.94E-07 0.000

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 337 253.2 216.5 268.900

lb/mmBtuO2 3.57E-02 2.64E-02 2.27E-02 0.028

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.0729 0.1119 0.0228 0.069

lb/mmBtuO2 7.73E-06 1.17E-05 2.39E-06 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.0343 0.026 0.0235 0.028

lb/mmBtuO2 3.64E-06 2.71E-06 2.46E-06 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.0173 0.015 0.0141 0.015

lb/mmBtuO2 1.83E-06 1.56E-06 1.48E-06 0.000

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.01 0.01 0.01 0.010

lb/mmBtuO2 1.06E-06 1.04E-06 1.05E-06 0.000

Location: Stack - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

lb/mmBtuO2 7.51E-01 8.82E-01 8.78E-01 0.837

ppm 3.57E+02 4.18E+02 3.75E+02 383.333

ppm@7%O2 2.96E+02 3.49E+02 3.16E+02 320.333

Location: Stack - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 2 1 3

Mass_mg 92.9 130.6 78.1 100.533

lb/mmBtuO2 1.91E-02 2.79E-02 1.63E-02 0.021

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 31.2 21.8 24.2 25.733

lb/mmBtuO2 6.66E-03 4.49E-03 5.05E-03 0.005

Thursday, January 20, 2011 Page 8 of 17
Ebensburg Power - ICR

9/2/2010

Process Run Data

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 161.5 131.2 115.1 135.933

lb/mmBtuO2 3.45E-02 2.70E-02 2.40E-02 0.029

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 62.1 60.1 61.2 61.133

lb/mmBtuO2 1.33E-02 1.24E-02 1.28E-02 0.013

Thursday, January 20, 2011 Page 9 of 17
Ebensburg Power - ICR

9/2/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Waste Bituminous (GOB) feed rate 136970 lbs./hr Test Run 1 for CO, 

THC, SO2 Testing 

Performed 

5/13/2010

0

1 Heat Input 760.96 MMBtu/hr 0

1 Steam Flow 480.31 klbs/hr 0

1 Mega Watt output 59.31 MW 0

1 Stack Temp 323 F 0

1 Stack Flow Rate 169995 scfm 0

1 Stack CO2 15.41 % 0

1 Stack O2 4.16 % 0

1 Stack Moisture 9.34 % 0 7:00-9:00 am

2 Waste Bituminous (GOB) feed rate 142400 lbs./hr Test Run 2 data 

for CO, THC SO2 

Testing Performed 

on 5/13/10

0

2 Heat Input 784.3 MMBtu/hr 0

2 Steam Flow 481.3 klbs/hr 0

2 Mega Watt output 59.39 MW 0

2 Stack Temp 316 F 0

2 Stack Flow Rate 175238 scfm 0

2 Stack CO2 15.37 % 0

2 Stack O2 4.24 % 0

2 Stack Moisture 9.14 % 0 10:00-12:00am

3 Waste Bituminous (GOB) feed rate 149300 lbs./hr Test Run 3 data 

for CO, THC and 

SO2 Testing 

Performed 5/13/10

0

3 Heat Input 778.2 MMBtu/hr 0

3 Steam Flow 477.96 klbs/hr 0

3 Mega Watt output 59.1 MW 0

3 Stack Temp 322 F 0

3 Stack Flow Rate 174233 scfm 0

3 Stack CO2 15.2 % 0

3 Stack O2 4.42 % 0

3 Stack Moisture 9.34 % 0 12:30-16:30

Thursday, January 20, 2011 Page 10 of 17
Ebensburg Power - ICR

9/2/2010

APCD Run Data

4 Waste Bituminous (GOB) feed rate 139990 lbs./hr Test Run 1 for 

M29 and OTM 

27/28 performed 

7/26/10

0

4 Heat Input 798.6 MMBtu/hr 0

4 Steam Flow 480.03 klbs/hr 0

4 Mega Watt output 58.51 MW 0

4 Stack Temp 328 F 0

4 Stack Flow Rate 181571 scfm 0

4 Stack CO2 15.49 % 0

4 Stack O2 4.06 % 0

4 Stack Moisture 8.41 % 0 13:00-19:00

5 Waste Bituminous (GOB) feed rate 143860 lbs./hr Test run 2 for M29 

and OTM 27/28 

performed 7/28/10

0

5 Heat Input 792.2 MMBtu/hr 0

5 Steam Flow 480.79 klbs/hr 0

5 Mega Watt output 58.69 MW 0

5 Stack Temp 328 F 0

5 Stack Flow Rate 179417 scfm 0

5 Stack CO2 15.77 % 0

5 Stack O2 3.74 % 0

5 Stack Moisture 9.1 % 0 7:30-13:45

6 Waste Bituminous (GOB) feed rate 142980 lbs./hr Test Run 3 for 

M29 and OTM 

27/28 performed 

7/29/10

0

6 Heat Input 803.96 MMBtu/hr 0

6 Steam Flow 481.96 klbs/hr 0

6 Mega Watt output 59.09 MW 0

6 Stack Temp 328 F 0

6 Stack Flow Rate 181080 scfm 0

6 Stack CO2 15.95 % 0

6 Stack O2 3.71 % 0

6 Stack Moisture 9.6 % 0 6:00-12:00

Run Name Value UOM Comments

Target

Value

1 BAGHOUSE 8.11 "H2O 0

Thursday, January 20, 2011 Page 11 of 17
Ebensburg Power - ICR

9/2/2010

Process Lab Run Data

2 BAGHOUSE 8.49 "H2O 0

3 BAGHOUSE 8.47 "H2O 0

4 BAGHOUSE 7.31 "H2O 0

5 BAGHOUSE 8.29 "H2O 0

6 BAGHOUSE 8.35 "H2O 0

1 DRY LIMESTONE INJECTION 32.23 Klb/Hr 0

2 DRY LIMESTONE INJECTION 31.4 Klb/Hr 0

3 DRY LIMESTONE INJECTION 33.51 Klb/Hr 0

4 DRY LIMESTONE INJECTION 33.54 Klb/Hr 0

5 DRY LIMESTONE INJECTION 31.44 Klb/Hr 0

6 DRY LIMESTONE INJECTION 37.15 Klb/Hr 0

Thursday, January 20, 2011 Page 12 of 17
Ebensburg Power - ICR

9/2/2010

Sampling / Stack Data Results Detail

Location Stack - 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

Thursday, January 20, 2011 Page 13 of 17
Ebensburg Power - ICR

9/2/2010

Location Stack - 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

Thursday, January 20, 2011 Page 14 of 17
Ebensburg Power - ICR

9/2/2010

Location Stack - Method 29

Average

Run Number 1 2 3

Test Date 7/26/2010 7/28/2010 7/29/2010

Run Start Time 1:10:00 PM 7:35:00 AM 6:10:00 AM

Run Finish Time 7:15:00 PM 1:44:00 PM 12:07:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 330 330 330

Nozzle Diameter, inches 0.223 0.223 0.223 0.223

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.0008 1.0008 1.0008 1.001

Barometric Pressure, inches of Mercury 30.21 30.09 30 30.100

Average Orifice Meter Differential, inches H2O 2.02 1.95 1.97 1.980

Dry Gas Meter Volume Sampled, cubic feet 267.783 263.319 265.617 265.573

Average Dry Gas Meter Temperature, °F 94.17 85.33 83.42 87.640

Dry Gas Meter Volume Sampled, dscf 259.084 257.827 260.227 259.046

Total Moisture Liquid collected, g 505 549 588 547.333

Volume of Water Vapor, standard cubic feet 23.77 25.84 27.68 25.763

Moisture Content of Stack Gas, % 8.40 9.11 9.61 9.040

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

Dry Mole Fraction 0.916 0.9089 0.9039 0.910

Carbon Dioxide, % 15.49 15.77 15.95 15.737

Oxygen, % 4.06 3.74 3.71 3.837

Carbon Monoxide & Nitrogen, % 80.45 80.49 80.34 80.427

Fuel Factor 1.09 1.09 1.08

Dry Molecular Weight, lb/lb-Mole 30.64 30.67 30.70 30.670

Wet Molecular weight, lb/lb-Mole 29.58 29.52 29.48 29.527

Flue Gas Static Pressure, inches of H2O -0.88 -0.91 -0.95 -0.913

Absolute Flue Gas Pressure, inches of Mercury 30.15 30.02 29.93 30.033

Average Stack Gas Temperature, °F 328.42 328.25 328.00 328.223

Average Velocity Head, inches of H2O 1.2199227237

5933

1.193273876

67091

1.217316470

44946

1.210

Average Stack Gas Velocity, feet/second 74.58 73.98 74.88 74.480

Stack Cross-Sectional Area, square feet 60.132 60.132 60.132 60.132

Dry Volumetric Flow Rate, dry scfm 166,332.4 163,044.6 163,680.1 164,352.367

Actual Wet Volumetric Flue Gas Flow Rate, acfm 269,078.7 266,913.9 270,161.0 268,717.867

Percent Isokinetic of Sampling Rate, % 104.6 106.2 106.8 105.867

Percent Excess Air, % 23.6 21.4 21.2 22.067

F-Factor, dscfm/MMBtu @ %O2 10041 10007 10165 10,071.000

Round Duct Diameter, inches 105 105 105

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Thursday, January 20, 2011 Page 15 of 17
Ebensburg Power - ICR

9/2/2010

Location Stack - 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

Thursday, January 20, 2011 Page 16 of 17
Ebensburg Power - ICR

9/2/2010

Location Stack - 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

Thursday, January 20, 2011 Page 17 of 17