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 02, 2011 Page 1 of 14
Facility Information:

Hardin Generator Project

Sugar Factory Road

Crow Agency MT 59022

Contact: Terry Hart

Phone: 406-638-9140

Fax:

Email: thart@coloradoenergy.com

Testing Company:

Emissions Measurement Company LLC

5160 Parfet Street

Unit A3

Wheat Ridge CO 80033

Contact:Matthew Parks

Phone: 303-495-3936

Fax: 888-605-0243

Email: mparks@stacktest.us

Air Permit Number:

55749

Permitted Source ID/Name:

PC1 Enter the Boiler ID of the tested boiler (left)

Permitted Maximum Process Rate:

N/A

Max. Normal Operation Process Rate:

N/A

Target Process Test Rate

N/A

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

 process flow diagram:

This description should describe the process and associated controls to differentiate this facility from, or document 

similarity with others of same SCC.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 3000300018 FRS #: 110038363623

SCC / Description 10100201 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Pulverized Coal: Wet 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

Stack Exit 108 0 0 0 1476 1524 4 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 3 120 0

Stack Exit Hydrogen Fluoride Method 26A 3 180 0

Stack Exit Hydrogen Chloride Method 26A 3 180 0

Filterable Particulate OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Wednesday, February 02, 2011 Page 2 of 14
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.

N/A

Total Particulate OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Total PM2.5 OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Organic Condensible 

Particulate

OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Inorganic (Aqueous) 

Condensible Part.

OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Filterable PM2.5 OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Stack Exit Arsenic Method 29 3 240 0

Stack Exit Beryllium Method 29 3 240 0

Stack Exit Cadmium Method 29 3 240 0

Stack Exit Chromium Method 29 3 240 0

Stack Exit Lead Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Antimony Method 29 3 240 0

Stack Exit Filterable Particulate Method 29 3 240 0

Stack Exit Selenium Method 29 3 240 0

Wednesday, February 02, 2011 Page 3 of 14
Sampling / Stack Data Results Summary

Location Stack Exit - 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

Location Stack Exit - Method 26A

Average

Run Number 26A1 26A2 26A3

Test Date 6/30/2010 7/2/2010 7/2/2010

Run Start Time 3:26:00 PM 7:51:00 

AM

11:45:00 AM

Run Finish Time 7:57:00 PM 11:03:00 

AM

2:50:00 PM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 105.140 104.957 104.192 104.763

Moisture Content of Stack Gas, % 16.76 16.59 16.91 16.753

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

Carbon Dioxide, % 12.6 12.8 12.4 12.600

Oxygen, % 6 5.8 6.2 6.000

Average Stack Gas Temperature, °F 215.25 219.21 219.79 218.083

Dry Volumetric Flow Rate, dry scfm 298,196.4 294,120.3 297,939.5 296,752.067

Actual Wet Volumetric Flue Gas Flow Rate, acfm 512,434.9 507,358.3 516,366.5 512,053.233

Percent Isokinetic of Sampling Rate, % 98.9 100.1 98.1 99.033

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 02, 2011 Page 4 of 14
Location Stack Exit - Method 29

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

Location Stack Exit - 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

Wednesday, February 02, 2011 Page 5 of 14
Emissions Summary

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 25A1 25A2 25A3

lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000

ppm 0.00E+00 0.00E+00 0.00E+00 0.000

ppm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 26A1 26A2 26A3

Mass_mg 0.5 0.512 0.5 0.504

Elb/hr 1.88E-01 1.90E-01 1.89E-01 0.189

lb/mmBtuO2 1.44E-04 1.46E-04 1.47E-04 0.000

mg/dscm 1.68E-01 1.72E-01 1.69E-01 0.170

mg/dscm@7%O2 1.57E-01 1.58E-01 1.60E-01 0.158

Compound: Hydrogen Fluoride

Average

RunNumber 26A1 26A2 26A3

Mass_mg 0.1 0.1 0.1 0.100

Elb/hr 3.75E-02 3.71E-02 3.78E-02 0.037

lb/mmBtuO2 2.88E-05 2.84E-05 2.94E-05 0.000

mg/dscm 3.36E-02 3.37E-02 3.39E-02 0.034

mg/dscm@7%O2 3.13E-02 3.10E-02 3.21E-02 0.031

Location: Stack Exit - Method 29

Compound: Antimony

Average

RunNumber 29-1 29-2 29-3

Mass_mg 0.003972 0.007652 0.007469 0.006

Elb/hr 1.14E-03 2.18E-03 2.11E-03 0.002

lb/mmBtuO2 8.59E-07 1.64E-06 1.56E-06 0.000

mg/dscm 9.83E-04 1.89E-03 1.80E-03 0.002

mg/dscm@7%O2 9.36E-04 1.79E-03 1.70E-03 0.001

Compound: Arsenic

Average

RunNumber 29-1 29-2 29-3

Mass_mg 0.0012 0.000239 0.000257 0.001

Elb/hr 3.44E-04 6.79E-05 7.25E-05 0.000

lb/mmBtuO2 2.60E-07 5.13E-08 5.38E-08 0.000

mg/dscm 2.97E-04 5.91E-05 6.20E-05 0.000

mg/dscm@7%O2 2.83E-04 5.59E-05 5.86E-05 0.000

Compound: Beryllium

Average

RunNumber 29-1 29-2 29-3

Mass_mg 0.0003 0.0003 0.000204 0.000

Wednesday, February 02, 2011 Page 6 of 14
Elb/hr 8.59E-05 8.53E-05 5.76E-05 0.000

lb/mmBtuO2 6.49E-08 6.44E-08 4.27E-08 0.000

mg/dscm 7.42E-05 7.42E-05 4.92E-05 0.000

mg/dscm@7%O2 7.06E-05 7.02E-05 4.65E-05 0.000

Compound: Cadmium

Average

RunNumber 29-1 29-2 29-3

Mass_mg 0.0000627 0.000338 0.00029 0.000

Elb/hr 1.80E-05 9.61E-05 8.19E-05 0.000

lb/mmBtuO2 1.36E-08 7.25E-08 6.07E-08 0.000

mg/dscm 1.55E-05 8.36E-05 7.00E-05 0.000

mg/dscm@7%O2 1.48E-05 7.91E-05 6.62E-05 0.000

Compound: Chromium

Average

RunNumber 29-1 29-2 29-3

Mass_mg 0.01473 0.0056 0.00601 0.009

Elb/hr 4.22E-03 1.59E-03 1.70E-03 0.003

lb/mmBtuO2 3.19E-06 1.20E-06 1.26E-06 0.000

mg/dscm 3.65E-03 1.38E-03 1.45E-03 0.002

mg/dscm@7%O2 3.48E-03 1.30E-03 1.37E-03 0.002

Compound: Filterable Particulate

Average

RunNumber 29-1 29-2 29-3

Mass_mg 38.1 97.8 79 71.633

Elb/hr 1.09E+01 2.78E+01 2.23E+01 20.333

lb/mmBtuO2 8.24E-03 2.10E-02 1.65E-02 0.015

mg/dscm 9.43E+00 2.42E+01 1.91E+01 17.577

mg/dscm@7%O2 8.98E+00 2.29E+01 1.81E+01 16.660

Compound: Lead

Average

RunNumber 29-1 29-2 29-3

Mass_mg 0.00389 0.0042 0.0067 0.005

Elb/hr 1.11E-03 1.19E-03 1.89E-03 0.001

lb/mmBtuO2 8.41E-07 9.01E-07 1.40E-06 0.000

mg/dscm 9.63E-04 1.04E-03 1.62E-03 0.001

mg/dscm@7%O2 9.17E-04 9.83E-04 1.53E-03 0.001

Compound: Manganese

Average

RunNumber 29-1 29-2 29-3

Mass_mg 0.0342 0.03801 0.04607 0.039

Elb/hr 9.80E-03 1.08E-02 1.30E-02 0.011

lb/mmBtuO2 7.40E-06 8.16E-06 9.65E-06 0.000

mg/dscm 8.46E-03 9.40E-03 1.11E-02 0.010

mg/dscm@7%O2 8.05E-03 8.89E-03 1.05E-02 0.009

Compound: Nickel

Average

RunNumber 29-1 29-2 29-3

Mass_mg 0.01475 0.00863 0.0048 0.009

Wednesday, February 02, 2011 Page 7 of 14
Process Run Data

Elb/hr 4.22E-03 2.45E-03 1.35E-03 0.003

lb/mmBtuO2 3.19E-06 1.85E-06 1.00E-06 0.000

mg/dscm 3.65E-03 2.13E-03 1.16E-03 0.002

mg/dscm@7%O2 3.48E-03 2.01E-03 1.10E-03 0.002

Compound: Selenium

Average

RunNumber 29-1 29-2 29-3

Mass_mg 0.003 0.003 0.003 0.003

Elb/hr 8.59E-04 8.53E-04 8.47E-04 0.001

lb/mmBtuO2 6.49E-07 6.44E-07 6.28E-07 0.000

mg/dscm 7.42E-04 7.42E-04 7.24E-04 0.001

mg/dscm@7%O2 7.06E-04 7.02E-04 6.85E-04 0.001

Location: Stack Exit - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 027-1 027-2 027-3

Mass_mg 26 31.6 43.3 33.633

lb/mmBtuO2 7.58E-03 8.90E-03 1.23E-02 0.010

Compound: Filterable PM2.5

Average

RunNumber 027-1 027-2 027-3

Mass_mg 4.6 6.8 6 5.800

lb/mmBtuO2 1.34E-03 1.91E-03 1.71E-03 0.002

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 027-1 027-2 027-3

Mass_mg 162 205.6 349.2 238.933

lb/mmBtuO2 4.72E-02 5.79E-02 9.93E-02 0.068

Compound: Organic Condensible Particulate

Average

RunNumber 027-1 027-2 027-3

Mass_mg 3.9 7.8 3.5 5.067

lb/mmBtuO2 1.14E-03 2.20E-03 9.96E-04 0.001

Compound: Total Particulate

Average

RunNumber 027-1 027-2 027-3

Mass_mg 191.9 245 396 277.633

lb/mmBtuO2 5.59E-02 6.90E-02 1.13E-01 0.079

Compound: Total PM2.5

Average

RunNumber 027-1 027-2 027-3

Mass_mg 170.5 220.2 358.7 249.800

lb/mmBtuO2 4.97E-02 6.20E-02 1.02E-01 0.071

Wednesday, February 02, 2011 Page 8 of 14
Process Run Data

Run Name Value UOM Comments

Target

Value

1 Average Heat Input 1199.2 MMBtu/hr 0 Test Run# 25A-1

1 Unit Gross Electrical Output 119 MW 0 Test Run# 25A-1

4 Average Heat Input 1182.5 MMBtu/hr 0 Test Run# 25A-2

4 FGD Scrubber Liquor Flow Rate 20 gal/min 0 Test Run# 25A-2

4 Sorbent Type and Sorbent Injection Rate (if 

applicable)

25.95 lb/hr 0 Test Run# 25A-2

4 Unit Gross Electrical Output 120 MW 0 Test Run# 25A-2

5 Average Heat Input 1185 MMBtu/hr 0 Test Run# 25A-3

5 FGD Scrubber Liquor Flow Rate 22.7 gal/min 0 Test Run# 25A-3

5 Sorbent Type and Sorbent Injection Rate (if 

applicable)

25.95 lb/hr 0 Test Run# 25A-3

5 Unit Gross Electrical Output 120 MW 0 Test Run# 25A-3

6 Average Heat Input 1127.2 MMBtu/hr 0 Test Run# 26A-1

6 FGD Scrubber Liquor Flow Rate 24.2 gal/min 0 Test Run# 26A-1

6 Sorbent Type and Sorbent Injection Rate (if 

applicable)

25.95 lb/hr 0 Test Run# 26A-1

6 Unit Gross Electrical Output 116 MW 0 Test Run# 26A-1

7 Average Heat Input 1202.6 MMBtu/hr 0 Test Run# 26A-2

7 FGD Scrubber Liquor Flow Rate 20.4 gal/min 0 Test Run# 26A-2

7 Sorbent Type and Sorbent Injection Rate (if 

applicable)

15.29 lb/hr 0 Test Run# 26A-2

7 Unit Gross Electrical Output 117 MW 0 Test Run# 26A-2

8 Average Heat Input 1266.9 MMBtu/hr 0 Test Run# 26A-3

8 FGD Scrubber Liquor Flow Rate 19.8 gal/min 0 Test Run# 26A-3

8 Sorbent Type and Sorbent Injection Rate (if 

applicable)

15.29 lb/hr 0 Test Run# 26A-3

8 Unit Gross Electrical Output 118 MW 0 Test Run# 26A-3

9 Average Heat Input 1181.9 MMBtu/hr 0 Test Run# 29-1

9 FGD Scrubber Liquor Flow Rate 22.4 gal/min 0 Test Run# 29-1

9 Sorbent Type and Sorbent Injection Rate (if 

applicable)

25.79 lb/hr 0 Test Run# 29-1

9 Unit Gross Electrical Output 120 MW 0 Test Run# 29-1

10 Average Heat Input 1191.9 MMBtu/hr 0 Test Run# 29-2

10 FGD Scrubber Liquor Flow Rate 29.6 gal/min 0 Test Run# 29-2

10 Sorbent Type and Sorbent Injection Rate (if 

applicable)

28.45 lb/hr 0 Test Run# 29-2

Wednesday, February 02, 2011 Page 9 of 14
APCD Run Data

Process Lab Run Data

10 Unit Gross Electrical Output 117 MW 0 Test Run# 29-2

11 Average Heat Input 1125.1 MMBtu/hr 0 Test Run# 29-3

11 FGD Scrubber Liquor Flow Rate 28.45 gal/min 0 Test Run# 29-3

11 Sorbent Type and Sorbent Injection Rate (if 

applicable)

25.2 lb/hr 0 Test Run# 29-3

11 Unit Gross Electrical Output 116 MW 0 Test Run# 29-3

12 Average Heat Input 1187.6 MMBtu/hr 0 Test Run# 027-1

12 FGD Scrubber Liquor Flow Rate 23.4 gal/min 0 Test Run# 027-1

12 Sorbent Type and Sorbent Injection Rate (if 

applicable)

25.95 lb/hr 0 Test Run# 027-1

12 Unit Gross Electrical Output 117 MW 0 Test Run# 027-1

13 Average Heat Input 1181.1 MMBtu/hr 0 Test Run# 027-2

13 FGD Scrubber Liquor Flow Rate 28.7 gal/min 0 Test Run# 027-2

13 Sorbent Type and Sorbent Injection Rate (if 

applicable)

28.45 lb/hr 0 Test Run# 027-2

13 Unit Gross Electrical Output 116 MW 0 Test Run# 027-2

14 Average Heat Input 1108.7 MMBtu/hr 0 Test Run# 027-3

14 FGD Scrubber Liquor Flow Rate 25.1 gal/min 0 Test Run# 027-3

14 Sorbent Type and Sorbent Injection Rate (if 

applicable)

28.45 lb/hr 0 Test Run# 027-3

14 Unit Gross Electrical Output 115 MW 0 Test Run# 027-3

Run Name Value UOM Comments

Target

Value

1 List all emissions control devices in order of 

process flow. Choose from

0 0

1 drop down lists. If not on list add description and 

provide detailed

0 0

1 desription in section 5a. 0 0

1 SCR (SELECTIVE CATALYTIC REDUCTION) 0 0

1 SPRAY DRYER 0 0

1 ACTIVATED CARBON ADSORPTION 0 0

Run Name Value UOM Comments

1 See 4b Comments. 0

Wednesday, February 02, 2011 Page 10 of 14
Sampling / Stack Data Results Detail

Location Stack Exit - 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

Wednesday, February 02, 2011 Page 11 of 14
Location Stack Exit - Method 26A

Average

Run Number 26A1 26A2 26A3

Test Date 6/30/2010 7/2/2010 7/2/2010

Run Start Time 3:26:00 PM 7:51:00 AM 11:45:00 AM

Run Finish Time 7:57:00 PM 11:03:00 AM 2:50:00 PM

Net Traversing Points 24 24 24

Net Run Time, minutes 180 180 180

Nozzle Diameter, inches 0.152 0.152 0.152 0.152

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9966 0.9966 0.9966 0.997

Barometric Pressure, inches of Mercury 26.88 26.88 26.88 26.880

Average Orifice Meter Differential, inches H2O 1.38 1.37 1.38 1.377

Dry Gas Meter Volume Sampled, cubic feet 119.537 120.484 123.052 121.024

Average Dry Gas Meter Temperature, °F 79.50 84.71 100.42 88.210

Dry Gas Meter Volume Sampled, dscf 105.140 104.957 104.192 104.763

Total Moisture Liquid collected, g 449.8 443.7 450.3 447.933

Volume of Water Vapor, standard cubic feet 21.17 20.88 21.20 21.083

Moisture Content of Stack Gas, % 16.76 16.59 16.91 16.753

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

Dry Mole Fraction 0.8324 0.8341 0.8309 0.832

Carbon Dioxide, % 12.6 12.8 12.4 12.600

Oxygen, % 6 5.8 6.2 6.000

Carbon Monoxide & Nitrogen, % 81.4 81.4 81.4 81.400

Fuel Factor 1.18 1.18 1.19

Dry Molecular Weight, lb/lb-Mole 30.26 30.28 30.23 30.257

Wet Molecular weight, lb/lb-Mole 28.21 28.24 28.16 28.203

Flue Gas Static Pressure, inches of H2O -1.8 -1.8 -1.8 -1.800

Absolute Flue Gas Pressure, inches of Mercury 26.75 26.75 26.75 26.750

Average Stack Gas Temperature, °F 215.25 219.21 219.79 218.083

Average Velocity Head, inches of H2O 3.9056304353

591

3.810704466

52856

3.932225638

08577

3.883

Average Stack Gas Velocity, feet/second 134.25 132.92 135.28 134.150

Stack Cross-Sectional Area, square feet 63.617 63.617 63.617 63.617

Dry Volumetric Flow Rate, dry scfm 298,196.4 294,120.3 297,939.5 296,752.067

Actual Wet Volumetric Flue Gas Flow Rate, acfm 512,434.9 507,358.3 516,366.5 512,053.233

Percent Isokinetic of Sampling Rate, % 98.9 100.1 98.1 99.033

Percent Excess Air, % 38.7 37.0 40.6 38.767

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

Round Duct Diameter, inches 108 108 108

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 02, 2011 Page 12 of 14
Location Stack Exit - Method 29

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

Wednesday, February 02, 2011 Page 13 of 14
Location Stack Exit - 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

Wednesday, February 02, 2011 Page 14 of 14