Name: Marty Stange

Title: Environmental Engineer

Company: Hastings Utilities

Sign Date: 6/23/2010

Name: Chet Gutwein

Title: Engineer

Company: Airtech Environmental Services Inc.

Sign Date: 6/23/2010

Permitted Facility Representative / Date Testing Company Representative / Date

3197 Hastings Utilities

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 27, 2011 Page 1 of 32
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Facility Information:

Whelan Energy Center

4520 East South Street

Hastings NE 68901

Contact: Marty Stange

Phone: (402) 463-1371

Fax: (402) 462-3666

Email: mstange@hastingsutilities.com

Testing Company:

Airtech Environmental Services Inc.

601A Country Club Drive

Bensenville IL 60106

Contact: Kurt Wepprecht

Phone: (630) 860-4740

Fax: (630) 860-4745

Email: kwepprecht@airtechenv.com

Air Permit Number:

OPO8R1-027

Permitted Source ID/Name:

58048 WEC1-000060

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:

The process for WEC1 is Combustion of Coal in a tangentially fired boiler with Over-fire Air for Nox control. 

Excess O2 is maintained for CO control. The Unit has a ESP for PM control. No other pollution control is 

provided. We burn low sulfur coal for SO2 compliance.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 3100100042 FRS #: 110001505602

SCC / Description 10100212 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Pulverized Coal: Dry Bottom (Tangential) (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 148 0 0 148 90 44.4 4 24

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

% H2O Method 1 - 4 3 120 0 From Method 0010 

Runs

Stack Exit

Stack Exit Carbon Monoxide Method 10 3 120 0

Stack Exit Formaldehyde Method 0011 3 120 0

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

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The following describes any modifications and/or deviations to the applicable test 

methods. If alternative methods were requested, see the attachments for documentation 

of request AND approval, including dates.

The following is a list of the test methods that are to be used for this test program and their respective promulgation 

dates:

Methods 1 through 29 – August 1997

Method 30B – January 2008

Other Test Methods 27 and 28 – April 2009

SW-846 0010 – September 1986

SW-846 0011 – December 1996

SW-846 0030 – December 1996

Organic Condensible 

Particulate

OTM - 27/28 3 390 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Filterable Particulate OTM - 27/28 3 390 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Inorganic (Aqueous) 

Condensible Part.

OTM - 27/28 3 390 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Total PM2.5 OTM - 27/28 3 390 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Total Particulate OTM - 27/28 3 390 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Filterable PM2.5 OTM - 27/28 3 390 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Stack Exit Selenium Method 29 3 240 0

Stack Exit Antimony Method 29 3 240 0

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 Nickel Method 29 3 240 0

Filterable Particulate Method 29 3 240 0 The sample 

temperature exceeded 

the Method 

requirement for this 

test run.

Stack Exit

Stack Exit Cobalt Method 29 3 240 0

Stack Exit Phosphorus (yellow or white) Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Co2 Method 3A CO2 3 120 0

Stack Exit O2 Method 3A O2 3 120 0

Stack Exit Sulfur Dioxide Method 6C 3 120 0

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

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Sampling / Stack Data Results Summary

Location Stack Exit - Method 0011

Average

Run Number 1 2 3

Test Date 3/23/2010 3/23/2010 3/23/2010

Run Start Time 8:12:00 AM 11:24:00 

AM

2:22:00 PM

Run Finish Time 10:49:00 AM 1:50:00 PM 4:41:00 PM

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 75.488 73.507 72.411 73.802

Moisture Content of Stack Gas, % 11.31 12.47 11.38 11.720

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

Carbon Dioxide, % 13.4 13.5 13.5 13.467

Oxygen, % 5.9 6.03 6.07 6.000

Average Stack Gas Temperature, °F 320.92 324.71 323.50 323.043

Dry Volumetric Flow Rate, dry scfm 212,401.6 211,128.7 208,463.5 210,664.600

Actual Wet Volumetric Flue Gas Flow Rate, acfm 380,123.3 384,710.9 374,603.9 379,812.700

Percent Isokinetic of Sampling Rate, % 103.0 100.9 100.6 101.500

F-Factor, dscfm/MMBtu @ %O2 9890 9890 9890 9,890.000

Fw 11033 11033 11033 11,033.000

Fc 1908 1908 1908 1,908.000

Thursday, January 27, 2011 Page 4 of 32
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Location Stack Exit - Method 1 - 4

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 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

Thursday, January 27, 2011 Page 5 of 32
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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

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 27, 2011 Page 6 of 32
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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

Thursday, January 27, 2011 Page 7 of 32
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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 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

Thursday, January 27, 2011 Page 8 of 32
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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

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

Thursday, January 27, 2011 Page 9 of 32
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Location Stack Exit - Method 6C 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 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

Thursday, January 27, 2011 Page 10 of 32
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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

Thursday, January 27, 2011 Page 11 of 32
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Emissions Summary

Location: Stack Exit - Method 0011

Compound: Formaldehyde

Average

RunNumber 1 2 3

Mass_mg 0.00338 0.0019 0.00181 0.002

lb/mmBtuO2 1.36E-06 7.92E-07 7.68E-07 0.000

ppm 1.27E-03 7.31E-04 7.07E-04 0.001

ppm@7%O2 1.18E-03 6.83E-04 6.63E-04 0.001

Location: Stack Exit - Method 1 - 4

Compound: % H2O

Average

RunNumber 1 2 3

Mass_mg 202100 205900 188900 198,966.667

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

Elb/hr 5.90E-02 4.56E-01 8.78E-01 0.464

lb/mmBtuO2 6.38E-05 5.01E-04 9.79E-04 0.001

ppm 6.37E-02 4.96E-01 9.66E-01 0.509

ppm@7%O2 5.91E-02 4.64E-01 9.05E-01 0.476

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

Elb/hr 0.00E+00 2.00E-01 3.64E-01 0.188

lb/mmBtuO2 0.00E+00 2.19E-04 4.05E-04 0.000

mg/dscm 0.00E+00 2.53E-01 4.66E-01 0.240

mg/dscm@7%O2 0.00E+00 2.37E-01 4.37E-01 0.225

ppm 0.00E+00 1.38E-01 2.54E-01 0.131

ppm@7%O2 0.00E+00 1.29E-01 2.38E-01 0.122

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 0.211 0.775 0.663 0.550

Elb/hr 5.31E-02 1.94E-01 1.66E-01 0.138

lb/mmBtuO2 6.32E-05 2.31E-04 1.93E-04 0.000

mg/dscm 7.16E-02 2.62E-01 2.21E-01 0.185

mg/dscm@7%O2 6.75E-02 2.47E-01 2.07E-01 0.174

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.804 0.839 1.02 0.888

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Elb/hr 2.02E-01 2.10E-01 2.55E-01 0.222

lb/mmBtuO2 2.41E-04 2.50E-04 2.97E-04 0.000

mg/dscm 2.73E-01 2.83E-01 3.40E-01 0.299

mg/dscm@7%O2 2.57E-01 2.67E-01 3.19E-01 0.281

Location: Stack Exit - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.00294 0.00097 0.00133 0.002

Elb/hr 5.59E-04 1.84E-04 2.58E-04 0.000

lb/mmBtuO2 6.20E-07 2.05E-07 2.94E-07 0.000

mg/dscm 7.02E-04 2.34E-04 3.37E-04 0.000

mg/dscm@7%O2 6.62E-04 2.19E-04 3.14E-04 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.00161 0.00171 0.00186 0.002

Elb/hr 3.06E-04 3.25E-04 3.60E-04 0.000

lb/mmBtuO2 3.39E-07 3.61E-07 4.11E-07 0.000

mg/dscm 3.84E-04 4.13E-04 4.71E-04 0.000

mg/dscm@7%O2 3.62E-04 3.87E-04 4.39E-04 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.000138 0.00013 0.000165 0.000

Elb/hr 2.62E-05 2.47E-05 3.20E-05 0.000

lb/mmBtuO2 2.91E-08 2.74E-08 3.65E-08 0.000

mg/dscm 3.29E-05 3.14E-05 4.18E-05 0.000

mg/dscm@7%O2 3.10E-05 2.95E-05 3.90E-05 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.000459 0.00028 0.000455 0.000

Elb/hr 8.73E-05 5.32E-05 8.82E-05 0.000

lb/mmBtuO2 9.67E-08 5.90E-08 1.01E-07 0.000

mg/dscm 1.10E-04 6.76E-05 1.15E-04 0.000

mg/dscm@7%O2 1.04E-04 6.34E-05 1.07E-04 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.00885 0.00796 0.00681 0.008

Elb/hr 1.68E-03 1.51E-03 1.32E-03 0.002

lb/mmBtuO2 1.87E-06 1.68E-06 1.50E-06 0.000

mg/dscm 2.11E-03 1.92E-03 1.72E-03 0.002

mg/dscm@7%O2 1.99E-03 1.80E-03 1.60E-03 0.002

Compound: Cobalt

Average

Thursday, January 27, 2011 Page 13 of 32
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RunNumber 1 2 3

Mass_mg 0.00158 0.00149 0.00115 0.001

Elb/hr 3.00E-04 2.83E-04 2.23E-04 0.000

lb/mmBtuO2 3.33E-07 3.14E-07 2.54E-07 0.000

mg/dscm 3.77E-04 3.60E-04 2.91E-04 0.000

mg/dscm@7%O2 3.56E-04 3.38E-04 2.71E-04 0.000

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 22.7 13.4 22.2 19.433

Elb/hr 4.32E+00 2.55E+00 4.30E+00 3.723

lb/mmBtuO2 4.78E-03 2.83E-03 4.91E-03 0.004

mg/dscm 5.42E+00 3.23E+00 5.62E+00 4.757

mg/dscm@7%O2 5.11E+00 3.03E+00 5.24E+00 4.460

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.00373 0.00337 0.00379 0.004

Elb/hr 7.09E-04 6.40E-04 7.35E-04 0.001

lb/mmBtuO2 7.86E-07 7.11E-07 8.37E-07 0.000

mg/dscm 8.91E-04 8.13E-04 9.59E-04 0.001

mg/dscm@7%O2 8.40E-04 7.63E-04 8.95E-04 0.001

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.00676 0.00667 0.00732 0.007

Elb/hr 1.29E-03 1.27E-03 1.42E-03 0.001

lb/mmBtuO2 1.42E-06 1.41E-06 1.62E-06 0.000

mg/dscm 1.61E-03 1.61E-03 1.85E-03 0.002

mg/dscm@7%O2 1.52E-03 1.51E-03 1.73E-03 0.002

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.00382 0.00439 0.00429 0.004

Elb/hr 7.26E-04 8.34E-04 8.31E-04 0.001

lb/mmBtuO2 8.05E-07 9.26E-07 9.48E-07 0.000

mg/dscm 9.12E-04 1.06E-03 1.09E-03 0.001

mg/dscm@7%O2 8.60E-04 9.94E-04 1.02E-03 0.001

Compound: Phosphorus (yellow or white)

Average

RunNumber 1 2 3

Mass_mg 0.0313 0.0363 0.0226 0.030

Elb/hr 5.95E-03 6.89E-03 4.38E-03 0.006

lb/mmBtuO2 6.60E-06 7.65E-06 4.99E-06 0.000

mg/dscm 7.47E-03 8.76E-03 5.72E-03 0.007

mg/dscm@7%O2 7.04E-03 8.22E-03 5.34E-03 0.007

Compound: Selenium

Average

Thursday, January 27, 2011 Page 14 of 32
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RunNumber 1 2 3

Mass_mg 0.000785 0.000992 0.00122 0.001

Elb/hr 1.49E-04 1.88E-04 2.36E-04 0.000

lb/mmBtuO2 1.65E-07 2.09E-07 2.70E-07 0.000

mg/dscm 1.87E-04 2.39E-04 3.09E-04 0.000

mg/dscm@7%O2 1.76E-04 2.24E-04 2.88E-04 0.000

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

Elb/hr 6.46E+02 6.64E+02 6.36E+02 648.667

lb/mmBtuO2 6.99E-01 7.28E-01 7.09E-01 0.712

mg/dscm 8.13E+02 8.39E+02 8.14E+02 822.000

mg/dscm@7%O2 7.54E+02 7.84E+02 7.63E+02 767.000

ppm 3.05E+02 3.15E+02 3.06E+02 308.667

ppm@7%O2 2.83E+02 2.94E+02 2.87E+02 288.000

Location: Stack Exit - Method 6C 3

Compound: Sulfur Dioxide

Average

Run 4 5 6

Elb/hr 5.74E+02 6.08E+02 6.24E+02 602.000

lb/mmBtuO2 6.79E-01 7.06E-01 7.32E-01 0.706

mg/dscm 7.69E+02 8.08E+02 8.38E+02 805.000

mg/dscm@7%O2 7.25E+02 7.58E+02 7.82E+02 755.000

ppm 2.89E+02 3.03E+02 3.15E+02 302.333

ppm@7%O2 2.73E+02 2.84E+02 2.94E+02 283.667

Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

Elb/hr 2.69E+02 2.66E+02 2.82E+02 272.333

lb/mmBtuO2 3.18E-01 3.09E-01 3.31E-01 0.319

mg/dscm 3.60E+02 3.53E+02 3.79E+02 364.000

mg/dscm@7%O2 3.39E+02 3.31E+02 3.54E+02 341.333

ppm 1.88E+02 1.85E+02 1.98E+02 190.333

ppm@7%O2 1.77E+02 1.74E+02 1.85E+02 178.667

Location: Stack Exit - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 19.8 19.1 13.3 17.400

lb/mmBtuO2 4.68E-03 4.53E-03 3.14E-03 0.004

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 11.2 10.2 1.05 7.483

lb/mmBtuO2 2.65E-03 2.42E-03 2.48E-04 0.002

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Process Run Data

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 8.7 2.7 9.3 6.900

lb/mmBtuO2 2.06E-03 6.41E-04 2.20E-03 0.002

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 2.2 3.6 3.8 3.200

lb/mmBtuO2 5.20E-04 8.55E-04 8.97E-04 0.001

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 30.7 25.4 26.4 27.500

lb/mmBtuO2 7.26E-03 6.03E-03 6.24E-03 0.007

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 22.1 16.5 14.1 17.567

lb/mmBtuO2 5.23E-03 3.92E-03 3.33E-03 0.004

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Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Bituminous Coal Burned 0.042 1000 Tons/hr 0.04

1 Average Heat Input 17587 MMBtu/hr 15000

1 Steam Output 450 1000 lb steam/hr 450

1 Flue Gas Flow Rate 1E+07 dscfm 1E+07

1 Flue Gas Carbon Dioxide Content 11.6 % 11.5

1 Flue Gas Sampling Point Temperature 315 Deg F 310

1 Unit Gross Electrical Output 1568 Mwe 1500

1 Unit Net Electric Generation 1442.3 MWh 1450

4 Bituminous Coal Burned 0.04 1000 Tons/hr 0.04

4 Average Heat Input 17570 MMBtu/hr 15000

4 Steam Output 450 1000 lb steam/hr 450

4 Flue Gas Flow Rate 1E+07 dscfm 1E+07

4 Flue Gas Carbon Dioxide Content 11.5 % 11.5

4 Flue Gas Sampling Point Temperature 310 Deg F 310

4 Unit Gross Electrical Output 1571 Mwe 1500

4 Unit Net Electric Generation 1446.5 MWh 1450

5 Bituminous Coal Burned 0.04 1000 Tons/hr 0.04

5 Average Heat Input 17452 MMBtu/hr 15000

5 Steam Output 449 1000 lb steam/hr 450

5 Flue Gas Flow Rate 1E+07 dscfm 1E+07

5 Flue Gas Carbon Dioxide Content 11.5 % 11.5

5 Flue Gas Sampling Point Temperature 312 Deg F 310

5 Unit Gross Electrical Output 1581 Mwe 1500

5 Unit Net Electric Generation 1456.3 MWh 1450

Run Name Value UOM Comments

Target

Value

1 ELECTROSTATIC PRECIPITATOR 0 lb/mmBtu 0.1

2 ELECTROSTATIC PRECIPITATOR 0 lb/mmBtu 0.1

3 ELECTROSTATIC PRECIPITATOR 0 lb/mmBtu 0.1

1 OVERFIRE AIR 0 ton/yr 1462.9

2 OVERFIRE AIR 0 ton/yr 1462.9

3 OVERFIRE AIR 0 ton/yr 1462.9

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Process Lab Run Data

Run Name Value UOM Comments

1 Fuel Higher Heating Value 11929 Btu/lb

1 Fuel Moisture 18.86 %

2 Fuel Higher Heating Value 11913 Btu/lb

2 Fuel Moisture 1915 %

3 Fuel Higher Heating Value 11920 Btu/lb

3 Fuel Moisture 1901 %

4 Fuel Higher Heating Value 11851 Btu/lb

4 Fuel Moisture 18.84 %

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6/23/2010

Sampling / Stack Data Results Detail

Location Stack Exit - Method 0011

Average

Run Number 1 2 3

Test Date 3/23/2010 3/23/2010 3/23/2010

Run Start Time 8:12:00 AM 11:24:00 AM 2:22:00 PM

Run Finish Time 10:49:00 AM 1:50:00 PM 4:41:00 PM

Net Traversing Points 24 24 24

Net Run Time, minutes 120 120 120

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 0.9989 0.9989 0.9989 0.999

Barometric Pressure, inches of Mercury 27.9 27.9 27.9 27.900

Average Orifice Meter Differential, inches H2O 1.42 1.38 1.35 1.383

Dry Gas Meter Volume Sampled, cubic feet 79.020 78.490 77.980 78.497

Average Dry Gas Meter Temperature, °F 56.75 67.06 71.52 65.110

Dry Gas Meter Volume Sampled, dscf 75.488 73.507 72.411 73.802

Total Moisture Liquid collected, g 204.5 222.5 197.6 208.200

Volume of Water Vapor, standard cubic feet 9.63 10.47 9.30 9.800

Moisture Content of Stack Gas, % 11.31 12.47 11.38 11.720

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

Dry Mole Fraction 0.8869 0.8753 0.8862 0.883

Carbon Dioxide, % 13.4 13.5 13.5 13.467

Oxygen, % 5.9 6.03 6.07 6.000

Carbon Monoxide & Nitrogen, % 80.7 80.47 80.43 80.533

Fuel Factor 1.12 1.10 1.10

Dry Molecular Weight, lb/lb-Mole 30.38 30.40 30.40 30.393

Wet Molecular weight, lb/lb-Mole 28.98 28.85 28.99 28.940

Flue Gas Static Pressure, inches of H2O -0.3 -0.3 -0.3 -0.300

Absolute Flue Gas Pressure, inches of Mercury 27.88 27.88 27.88 27.880

Average Stack Gas Temperature, °F 320.92 324.71 323.50 323.043

Average Velocity Head, inches of H2O 0.5642270657

74073

0.572575995

93724

0.546338239

329

0.561

Average Stack Gas Velocity, feet/second 53.03 53.67 52.26 52.987

Stack Cross-Sectional Area, square feet 119.468 119.468 119.468 119.468

Dry Volumetric Flow Rate, dry scfm 212,401.6 211,128.7 208,463.5 210,664.600

Actual Wet Volumetric Flue Gas Flow Rate, acfm 380,123.3 384,710.9 374,603.9 379,812.700

Percent Isokinetic of Sampling Rate, % 103.0 100.9 100.6 101.500

Percent Excess Air, % 38.3 39.6 40.0 39.300

F-Factor, dscfm/MMBtu @ %O2 9890 9890 9890 9,890.000

Round Duct Diameter, inches 148 148 148

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 11033 11033 11033 11,033.000

Fc 1908 1908 1908 1,908.000

Thursday, January 27, 2011 Page 19 of 32
3197 Hastings Utilities

6/23/2010

Location Stack Exit - Method 1 - 4

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 27, 2011 Page 20 of 32
3197 Hastings Utilities

6/23/2010

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

Thursday, January 27, 2011 Page 21 of 32
3197 Hastings Utilities

6/23/2010

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

Thursday, January 27, 2011 Page 22 of 32
3197 Hastings Utilities

6/23/2010

Location Stack Exit - Method 26A

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 27, 2011 Page 23 of 32
3197 Hastings Utilities

6/23/2010

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

Thursday, January 27, 2011 Page 24 of 32
3197 Hastings Utilities

6/23/2010

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

Thursday, January 27, 2011 Page 25 of 32
3197 Hastings Utilities

6/23/2010

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

Thursday, January 27, 2011 Page 26 of 32
3197 Hastings Utilities

6/23/2010

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

Thursday, January 27, 2011 Page 27 of 32
3197 Hastings Utilities

6/23/2010

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

Thursday, January 27, 2011 Page 28 of 32
3197 Hastings Utilities

6/23/2010

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

Thursday, January 27, 2011 Page 29 of 32
3197 Hastings Utilities

6/23/2010

Location Stack Exit - Method 6C 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

Thursday, January 27, 2011 Page 30 of 32
3197 Hastings Utilities

6/23/2010

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

Thursday, January 27, 2011 Page 31 of 32
3197 Hastings Utilities

6/23/2010

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

Thursday, January 27, 2011 Page 32 of 32