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 31
Facility Information:

OH_WH Zimmer Unit 1

1781 US Route 52

Moscow OH 45153

Contact: Jon Hays

Phone: 317-838-4445

Fax: 317-8382490

Email: jon.hays@duke.energy.com

Testing Company:

AECOM

2 Technology Park Drive

Westford MA 01886

Contact: Patrick Ford

Phone: 978-589-3427

Fax: 978-589-3100

Email: pat.ford@aecom.com

Air Permit Number: Permitted Source ID/Name:

Unit 1 No. 2 Fuel Oil/Coal-Fired Electric Utility Boilers

Permitted Maximum Process Rate:

12656

Max. Normal Operation Process Rate:

12656

Target Process Test Rate

12656

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 #: 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

Stack Exit 512 0 0 0 8 2 4 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Exit % H2O Method 1 - 4 3 60 0

Stack Exit Carbon Monoxide Method 10 4 120 0

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 3 120 0

Stack Exit Hydrogen Fluoride Method 26A 3 60 0

Stack Exit Hydrogen Chloride Method 26A 3 60 0

Stack Exit Arsenic Method 29 3 180 0

Stack Exit Manganese Method 29 3 180 0

Wednesday, February 02, 2011 Page 2 of 31
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.

EPA Method 26A was modified to include the provisions cited in Method CTM-033 to allow for the collection and 

analysis of HCN. Also, a higher strength NaOH was used in order to maintain the pH at a level that would ensure 

good HCN collection efficiency. This involved using 100 ml of 6N NaOH in the first impinger and 100 ml each of 

2N NaOH in impingers 3 and 4. The sample time was also reduced to 1-hour as allowed by EPA (see FAQ's section 

on the ICR website) again to ensure that the pH of the absorbing solution remained high.

Stack Exit Lead Method 29 3 180 0

Stack Exit Antimony Method 29 3 180 0

Stack Exit Beryllium Method 29 3 180 0

Stack Exit Cobalt Method 29 3 180 0

Stack Exit Chromium Method 29 3 180 0

Stack Exit Selenium Method 29 3 180 0

Stack Exit Cadmium Method 29 3 180 0

Stack Exit Nickel Method 29 3 180 0

Stack Exit O2 Method 3A O2 3 60 0

Stack Exit Co2 Method 3A CO2 3 60 0

Stack Exit Total Particulate Method 5/OTM-28 3 180 0

Stack Exit Filterable Particulate Method 5/OTM-28 3 180 0

Organic Condensible 

Particulate

Stack Exit Method 5/OTM-28 3 180 0

Inorganic (Aqueous) 

Condensible Part.

Stack Exit Method 5/OTM-28 3 180 0

Stack Exit Sulfur Dioxide Method 6C 3 60 0

Stack Exit Nitrogen oxides (NOx) Method 7E 3 180 0

Wednesday, February 02, 2011 Page 3 of 31
Sampling / Stack Data Results Summary

Location Stack Exit - 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 Exit - Method 10 3

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

Wednesday, February 02, 2011 Page 4 of 31
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 1 2 3

Test Date 4/20/2010 4/20/2010 4/20/2010

Run Start Time 9:28:00 AM 12:38:00 

PM

3:15:00 PM

Run Finish Time 12:07:00 PM 2:51:00 

PM

5:28:00 PM

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 98.410 97.142 96.138 97.230

Moisture Content of Stack Gas, % 14.16 14.83 14.94 14.643

Moisture Saturation at Stack Gas Temperature, % 15.14 15.14 15.14 15.140

Carbon Dioxide, % 12.51 12.51 12.48 12.500

Oxygen, % 6.81 6.78 6.77 6.787

Average Stack Gas Temperature, °F 129.00 129.00 129.00 129.000

Dry Volumetric Flow Rate, dry scfm 3,363,483.4 3,274,888.

2

3,263,034.7 3,300,468.76

7

Actual Wet Volumetric Flue Gas Flow Rate, acfm 4,500,356.6 4,416,285.

9

4,405,991.6 4,440,878.03

3

Percent Isokinetic of Sampling Rate, % 103.9 105.4 104.6 104.633

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 5 of 31
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 - 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

Wednesday, February 02, 2011 Page 6 of 31
Location Stack Exit - Method 3A CO2 3

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 3A CO2 3 6

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

Wednesday, February 02, 2011 Page 7 of 31
Location Stack Exit - 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 Stack Exit - Method 3A O2 3

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

Wednesday, February 02, 2011 Page 8 of 31
Location Stack Exit - Method 3A O2 3 6

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 5/OTM-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 9 of 31
Location Stack Exit - 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

Location Stack Exit - Method 7E

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

Wednesday, February 02, 2011 Page 10 of 31
Emissions Summary

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run M26A-1 M26A-2 M26A-3

Elb/hr 7.27E+01 2.07E+02 2.06E+02 161.900

lb/mmBtuO2 5.23E-03 1.52E-02 1.52E-02 0.012

ppm 4.96E+00 1.45E+01 1.45E+01 11.320

ppm@7%O2 4.89E+00 1.43E+01 1.43E+01 11.163

Location: Stack Exit - Method 10 3

Compound: Carbon Monoxide

Average

Run Organic-1 Organic-2 Organic-3

Elb/hr 1.05E+02 2.78E+02 2.61E+02 214.667

lb/mmBtuO2 7.79E-03 2.09E-02 1.94E-02 0.016

ppm 7.34E+00 1.96E+01 1.83E+01 15.080

ppm@7%O2 7.29E+00 1.95E+01 1.81E+01 14.963

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 1.04E-03 1.94E-04 5.00E-04 0.001

ppm 6.23E-01 1.16E-01 3.00E-01 0.346

ppm@7%O2 6.19E-01 1.15E-01 2.97E-01 0.344

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 2.84 2.44 2.74 2.673

Elb/hr 1.28E+01 1.09E+01 1.23E+01 12.000

lb/mmBtuO2 9.23E-04 8.02E-04 9.09E-04 0.001

mg/dscm 1.02E+00 8.87E-01 1.01E+00 0.972

mg/dscm@7%O2 1.01E+00 8.73E-01 9.94E-01 0.959

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.6 0.43 0.421 0.484

Elb/hr 2.71E+00 1.92E+00 1.89E+00 2.173

lb/mmBtuO2 1.95E-04 1.41E-04 1.40E-04 0.000

mg/dscm 2.15E-01 1.56E-01 1.55E-01 0.175

mg/dscm@7%O2 2.12E-01 1.54E-01 1.52E-01 0.173

Location: Stack Exit - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Wednesday, February 02, 2011 Page 11 of 31
Mass_mg 0.00028 0.0005 0.00059 0.000

Elb/hr 8.42E-04 1.47E-03 1.75E-03 0.001

lb/mmBtuO2 6.11E-08 1.07E-07 1.28E-07 0.000

ug/dscm 6.67E-02 1.18E-01 1.40E-01 0.108

ug/dscm@7%O2 6.65E-02 1.17E-01 1.39E-01 0.108

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.0083 0.0122 0.0147 0.012

Elb/hr 2.50E-02 3.59E-02 4.36E-02 0.035

lb/mmBtuO2 1.81E-06 2.62E-06 3.18E-06 0.000

ug/dscm 1.98E+00 2.87E+00 3.48E+00 2.777

ug/dscm@7%O2 1.97E+00 2.86E+00 3.47E+00 2.767

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.00007 0.00013 0.00012 0.000

Elb/hr 2.11E-04 3.83E-04 3.56E-04 0.000

lb/mmBtuO2 1.53E-08 2.79E-08 2.60E-08 0.000

ug/dscm 1.67E-02 3.06E-02 2.84E-02 0.025

ug/dscm@7%O2 1.67E-02 3.04E-02 2.83E-02 0.025

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.00122 0.00236 0.0093 0.004

Elb/hr 3.67E-03 6.95E-03 2.76E-02 0.013

lb/mmBtuO2 2.66E-07 5.07E-07 2.01E-06 0.000

ug/dscm 2.91E-01 5.56E-01 2.20E+00 1.016

ug/dscm@7%O2 2.90E-01 5.53E-01 2.19E+00 1.011

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.0527 0.0854 0.0503 0.063

Elb/hr 1.59E-01 2.52E-01 1.49E-01 0.187

lb/mmBtuO2 1.15E-05 1.84E-05 1.09E-05 0.000

ug/dscm 1.26E+01 2.01E+01 1.19E+01 14.867

ug/dscm@7%O2 1.26E+01 2.00E+01 1.18E+01 14.800

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.0011 0.0043 0.0012 0.002

Elb/hr 3.31E-03 1.27E-02 3.56E-03 0.007

lb/mmBtuO2 2.40E-07 9.24E-07 2.60E-07 0.000

ug/dscm 2.62E-01 1.01E+00 2.84E-01 0.519

ug/dscm@7%O2 2.61E-01 1.00E+00 2.83E-01 0.515

Compound: Lead

Average

RunNumber 1 2 3

Wednesday, February 02, 2011 Page 12 of 31
Mass_mg 0.00427 0.00357 0.00667 0.005

Elb/hr 1.28E-02 1.05E-02 1.98E-02 0.014

lb/mmBtuO2 9.31E-07 7.67E-07 1.44E-06 0.000

ug/dscm 1.02E+00 8.40E-01 1.58E+00 1.147

ug/dscm@7%O2 1.02E+00 8.36E-01 1.57E+00 1.142

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.0139 0.0172 0.0159 0.016

Elb/hr 4.18E-02 5.07E-02 4.71E-02 0.047

lb/mmBtuO2 3.03E-06 3.70E-06 3.44E-06 0.000

ug/dscm 3.31E+00 4.05E+00 3.76E+00 3.707

ug/dscm@7%O2 3.30E+00 4.03E+00 3.74E+00 3.690

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.0338 0.0694 0.0418 0.048

Elb/hr 1.02E-01 2.04E-01 1.24E-01 0.143

lb/mmBtuO2 7.37E-06 1.49E-05 9.04E-06 0.000

ug/dscm 8.06E+00 1.63E+01 9.89E+00 11.417

ug/dscm@7%O2 8.04E+00 1.62E+01 9.85E+00 11.363

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.2012 0.2347 0.3127 0.250

Elb/hr 6.05E-01 6.91E-01 9.27E-01 0.741

lb/mmBtuO2 4.39E-05 5.05E-05 6.76E-05 0.000

ug/dscm 4.80E+01 5.52E+01 7.40E+01 59.067

ug/dscm@7%O2 4.79E+01 5.49E+01 7.37E+01 58.833

Location: Stack Exit - Method 5/OTM-28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 38.2 50.1 39.8 42.700

Elb/hr 1.15E+02 1.52E+02 1.21E+02 129.333

gr/dscf 4.01E-03 5.28E-03 4.18E-03 0.004

gr/dscf@7%O2 4.00E-03 5.25E-03 4.16E-03 0.004

lb/mmBtuO2 8.40E-03 1.10E-02 8.75E-03 0.009

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 128 210 182 173.333

Elb/hr 3.84E+02 6.37E+02 5.55E+02 525.333

gr/dscf 1.34E-02 2.21E-02 1.91E-02 0.018

gr/dscf@7%O2 1.34E-02 2.20E-02 1.90E-02 0.018

lb/mmBtuO2 2.82E-02 4.63E-02 4.00E-02 0.038

Wednesday, February 02, 2011 Page 13 of 31
Process Run Data

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 25 5.9 6.7 12.533

Elb/hr 7.50E+01 1.79E+01 2.04E+01 37.767

gr/dscf 2.63E-03 6.22E-04 7.04E-04 0.001

gr/dscf@7%O2 2.62E-03 6.19E-04 7.01E-04 0.001

lb/mmBtuO2 5.50E-03 1.30E-03 1.47E-03 0.003

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 191.2 266 228.5 228.567

Elb/hr 5.74E+02 8.07E+02 6.97E+02 692.667

gr/dscf 2.01E-02 2.80E-02 2.40E-02 0.024

gr/dscf@7%O2 2.00E-02 2.79E-02 2.39E-02 0.024

lb/mmBtuO2 4.21E-02 5.86E-02 5.02E-02 0.050

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

Elb/hr 6.46E+03 4.89E+03 5.29E+03 5,546.667

lb/mmBtuO2 4.64E-01 3.60E-01 3.90E-01 0.405

ppm 1.92E+02 1.50E+02 1.62E+02 168.000

ppm@7%O2 1.89E+02 1.48E+02 1.59E+02 165.333

Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

Elb/hr 1.42E+03 1.44E+03 1.57E+03 1,476.667

lb/mmBtuO2 1.02E-01 1.06E-01 1.16E-01 0.108

ppm 5.91E+01 6.16E+01 6.72E+01 62.633

ppm@7%O2 5.83E+01 6.06E+01 6.61E+01 61.667

Wednesday, February 02, 2011 Page 14 of 31
Process Run Data

Run Name Value UOM Comments

Target

Value

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

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

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

4 Heat Input Million Btus/million BTU using O2 0 0

1 Average Heat Input 0 MMBtu/hr 0

2 Average Heat Input 0 MMBtu/hr 0

3 Average Heat Input 0 MMBtu/hr 0

4 Average Heat Input 0 MMBtu/hr 0

1 Steam Output 0 1000 lb steam/hr 0

2 Steam Output 0 1000 lb steam/hr 0

3 Steam Output 0 1000 lb steam/hr 0

4 Steam Output 0 1000 lb steam/hr 0

1 Synfuel Firing Rate 0 1000 Tons/hr 0

2 Synfuel Firing Rate 0 1000 Tons/hr 0

3 Synfuel Firing Rate 0 1000 Tons/hr 0

4 Synfuel Firing Rate 0 1000 Tons/hr 0

1 Petroleum Coke Firing Rate 0 1000 Tons/hr 0

2 Petroleum Coke Firing Rate 0 1000 Tons/hr 0

3 Petroleum Coke Firing Rate 0 1000 Tons/hr 0

4 Petroleum Coke Firing Rate 0 1000 Tons/hr 0

1 Coal Gas Firing Rate 0 Ft^3/min 0

2 Coal Gas Firing Rate 0 Ft^3/min 0

3 Coal Gas Firing Rate 0 Ft^3/min 0

4 Coal Gas Firing Rate 0 Ft^3/min 0

1 Fuel Oil Firing Rate 0 gal/hr 0

2 Fuel Oil Firing Rate 0 gal/hr 0

3 Fuel Oil Firing Rate 0 gal/hr 0

4 Fuel Oil Firing Rate 0 gal/hr 0

1 Flue Gas Flow Rate 0 0

4 Flue Gas Flow Rate 0 0

1 Pressure Drop Across FGD (if applicable) 0 in H20 0

4 Pressure Drop Across FGD (if applicable) 0 in H20 0

1 FGD Scrubber Liquor pH 0 pH 0

Wednesday, February 02, 2011 Page 15 of 31
APCD Run Data

Process Lab Run Data

4 FGD Scrubber Liquor pH 0 pH 0

1 FGD Scrubber Liquor Flow Rate 0 gal/min 0

4 FGD Scrubber Liquor Flow Rate 0 gal/min 0

1 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

4 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

1 Flue Gas Oxygen Content 0 % 0

4 Flue Gas Oxygen Content 0 % 0

1 Flue Gas Carbon Dioxide Content 0 % 0

4 Flue Gas Carbon Dioxide Content 0 % 0

1 Flue Gas Moisture Content 0 % 0

4 Flue Gas Moisture Content 0 % 0

1 Flue Gas Sampling Point Temperature 0 Deg F 0

4 Flue Gas Sampling Point Temperature 0 Deg F 0

1 Flue Gas Pressure 0 atm 0

4 Flue Gas Pressure 0 atm 0

1 Standard Pressure 0 atm 0

4 Standard Pressure 0 atm 0

1 Standard Temperature 0 Deg F 0

4 Standard Temperature 0 Deg F 0

1 Unit Gross Electrical Output 0 Mwe 0

4 Unit Gross Electrical Output 0 Mwe 0

1 Unit Net Electric Generation 0 MWh 0

4 Unit Net Electric Generation 0 MWh 0

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

Run Name Value UOM Comments

1 Fuel Higher Heating Value 0 Btu/lb

1 Fuel Moisture 0 %

Wednesday, February 02, 2011 Page 16 of 31
1 Ultimate/Proximate Analysis 0

1 Fuel Chlorine Content 0 mg/kg

1 Fuel Fluorine Content 0 mg/kg

1 Metals Content 0 mg/kg

Wednesday, February 02, 2011 Page 17 of 31
Sampling / Stack Data Results Detail

Location Stack Exit - 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

Wednesday, February 02, 2011 Page 18 of 31
Location Stack Exit - Method 10 3

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 19 of 31
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 20 of 31
Location Stack Exit - Method 26A

Average

Run Number 1 2 3

Test Date 4/20/2010 4/20/2010 4/20/2010

Run Start Time 9:28:00 AM 12:38:00 PM 3:15:00 PM

Run Finish Time 12:07:00 PM 2:51:00 PM 5:28:00 PM

Net Traversing Points 24 24 24

Net Run Time, minutes 120 120 120

Nozzle Diameter, inches 0.248 0.248 0.248 0.248

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.025 1.025 1.025 1.025

Barometric Pressure, inches of Mercury 29.1 29.1 29.1 29.100

Average Orifice Meter Differential, inches H2O 2.26 2.25 2.23 2.247

Dry Gas Meter Volume Sampled, cubic feet 97.682 98.025 98.453 98.053

Average Dry Gas Meter Temperature, °F 65.46 74.17 82.08 73.903

Dry Gas Meter Volume Sampled, dscf 98.410 97.142 96.138 97.230

Total Moisture Liquid collected, g 344.8 359.3 358.7 354.267

Volume of Water Vapor, standard cubic feet 16.23 16.91 16.88 16.673

Moisture Content of Stack Gas, % 14.16 14.83 14.94 14.643

Moisture Saturation at Stack Gas Temperature, % 15.14 15.14 15.14 15.140

Dry Mole Fraction 0.8584 0.8517 0.8506 0.854

Carbon Dioxide, % 12.51 12.51 12.48 12.500

Oxygen, % 6.81 6.78 6.77 6.787

Carbon Monoxide & Nitrogen, % 80.68 80.71 80.75 80.713

Fuel Factor 1.13 1.13 1.13

Dry Molecular Weight, lb/lb-Mole 30.27 30.27 30.27 30.270

Wet Molecular weight, lb/lb-Mole 28.53 28.45 28.44 28.473

Flue Gas Static Pressure, inches of H2O -0.51 -0.48 -0.51 -0.500

Absolute Flue Gas Pressure, inches of Mercury 29.06 29.06 29.06 29.060

Average Stack Gas Temperature, °F 129.00 129.00 129.00 129.000

Average Velocity Head, inches of H2O 0.7512696196

08125

0.721259583

317396

0.717879788

010599

0.730

Average Stack Gas Velocity, feet/second 52.46 51.48 51.36 51.767

Stack Cross-Sectional Area, square feet 1,429.774 1,429.774 1,429.774 1,429.774

Dry Volumetric Flow Rate, dry scfm 3,363,483.4 3,274,888.2 3,263,034.7 3,300,468.7

67

Actual Wet Volumetric Flue Gas Flow Rate, acfm 4,500,356.6 4,416,285.9 4,405,991.6 4,440,878.0

33

Percent Isokinetic of Sampling Rate, % 103.9 105.4 104.6 104.633

Percent Excess Air, % 47.0 46.7 46.5 46.733

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

Round Duct Diameter, inches 512 512 512

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 21 of 31
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 22 of 31
Location Stack Exit - 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

Wednesday, February 02, 2011 Page 23 of 31
Location Stack Exit - Method 3A CO2 3

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 24 of 31
Location Stack Exit - Method 3A CO2 3 6

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 25 of 31
Location Stack Exit - 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

Wednesday, February 02, 2011 Page 26 of 31
Location Stack Exit - Method 3A O2 3

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 27 of 31
Location Stack Exit - Method 3A O2 3 6

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 28 of 31
Location Stack Exit - Method 5/OTM-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 29 of 31
Location Stack Exit - 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

Wednesday, February 02, 2011 Page 30 of 31
Location Stack Exit - Method 7E

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 31 of 31