### Name:

Title: Company: Sign Date: Name: Title: Company: Sign Date: Permitted Facility Representative / Date Testing Company Representative / Date 

## 2010 EGU MACT ICR - CIPCO Fair#2

Final Test Report for

/ / Based on information and belief formed after reasonable inquiry, I certify that the statements and information in this test report are true, accurate, and complete. I have reviewed all testing details and results in this test report and hereby certify that the test report is authentic and accurate.

Saturday, January 22, 2011 Page 1 of 28

### 2010 EGU MACT ICR - CIPCO Fair#2

Facility Information:

Fair Station 3800 Highway 22

Muscatine IA
Contact: Sam Stineman

Phone: 319-366-8011

Fax: 319-366-6328

Email: sam.stineman@cipco.net Testing Company:

Platt Environmental 1520 Kensington Road

Suite 204

Oak Brook IL 60523-2141
Contact: Eric Ehlers

Phone: 630-521-9400

Fax: 630-521-9494

Email: EEhlers@plattenv.com

Air Permit Number:
1218 Permitted Source ID/Name:
Fair Station Unit 2 2

Permitted Maximum Process Rate:
N/A Max. Normal Operation Process Rate:
N/A Target Process Test Rate 36,0000 lb/hr

Description of the source (including control equipment). Please see the attachments for source or process flow diagram: Fair Station Unit 2 is a wall fired, dry bottom pulverized coal fired boiler capable of approximately 500mmBTU/hr. All fuel at the facility comes from Illinois Basin mines and is bituminous. The unit has an electrostatic precipitator to control particulate and low NOx burners. Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information: AFS #: CIPCO Fair Station FRS #: 110028167702

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 78 0 0 4 0 1 0 0

Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location
% H2O Method 1 - 4 3 180 0 Stack Exit Carbon Monoxide Method 10 3 120 0 Stack Exit Regulation Description Compound Limit Unit Acid Rain Program (Calendar Year Average) Nitrogen oxides (NOx) 0.46 lb/million BTU using CO2 Title V - Particulate Matter Total Particulate 0.43 lb/million BTU using CO2 Title V - SO2 Sulfur Dioxide 6 lb/million BTU using CO2



### Saturday, January 22, 2011 Page 2 of 28

### 2010 EGU MACT ICR - CIPCO Fair#2

Formaldehyde Method 0011 3 120 0 Stack Exit 2,3,7,8-TCDD Method 23 3 480 0 Stack Exit 1,2,3,7,8-PeCDD Method 23 3 480 0 Stack Exit 1,2,3,4,7,8-HxCDD Method 23 3 480 0 Stack Exit 1,2,3,6,7,8-HxCDD Method 23 3 480 0 Stack Exit 1,2,3,7,8,9-HxCDD Method 23 3 480 0 Stack Exit 1,2,3,4,6,7,8-HpCDD Method 23 3 480 0 Stack Exit OCDD Method 23 3 480 0 Stack Exit 2,3,7,8-TCDF Method 23 3 480 0 Stack Exit 1,2,3,7,8-PeCDF Method 23 3 480 0 Stack Exit 2,3,4,7,8-PeCDF Method 23 3 480 0 Stack Exit 1,2,3,4,7,8-HxCDF Method 23 3 480 0 Stack Exit 1,2,3,6,7,8-HxCDF Method 23 3 480 0 Stack Exit 2,3,4,6,7,8-HxCDF Method 23 3 480 0 Stack Exit 1,2,3,7,8,9-HxCDF Method 23 3 480 0 Stack Exit 1,2,3,4,6,7,8-HpCDF Method 23 3 480 0 Stack Exit 1,2,3,4,7,8,9-HpCDF Method 23 3 480 0 Stack Exit OCDF Method 23 3 480 0 Stack Exit Other TCDD Method 23 0 Stack Exit Other PeCDD Method 23 0 Stack Exit Other HxCDD Method 23 0 Stack Exit Other HpCDD Method 23 0 Stack Exit Other TCDF Method 23 0 Stack Exit Other PeCDF Method 23 0 Stack Exit Other HxCDF Method 23 0 Stack Exit Other HpCDF Method 23 0 Stack Exit Total Dioxins Method 23 3 480 0 Stack Exit Total Furans Method 23 3 480 0 Stack Exit 3,3',4,4'-TCB (PCB77) Method 23 3 480 0 Stack Exit 3,4,4',5-TCB (PCB81) Method 23 3 480 0 Stack Exit 2,3,3',4,4'-PeCB (PCB105) Method 23 3 480 0 Stack Exit 2,3,4,4',5-PeCB (PCB114) Method 23 3 480 0 Stack Exit 2,3',4,4',5-PeCB (PCB118) Method 23 3 480 0 Stack Exit 2',3,4,4',5-PeCB (PCB123) Method 23 3 480 0 Stack Exit 3,3',4,4',5-PeCB (PCB126) Method 23 3 480 0 Stack Exit 2,3,3',4,4',5/2,3,3',4,4',5'-

HxCB (PCBs156/157) Method 23 3 480 0 Stack Exit

2,3',4,4',5,5'-HxCB (PCB167) Method 23 3 480 0 Stack Exit 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 480 0 Stack Exit 2,3,3',4,4',5,5'-HpCB

(PCB189) Method 23 3 480 0 Stack Exit

Total PCBs Method 23 3 480 0 Stack Exit Total TEQ Method 23 3 480 0 Stack Exit Total organic compounds

(TOC) as Propane Method 25A 3 120 0 Stack Exit

Hydrogen Fluoride Method 26 3 180 0 Stack Exit Hydrogen Chloride Method 26 3 180 0 Stack Exit Hydrogen Fluoride Method 26A 3 180 0 Stack Exit Hydrogen Chloride Method 26A 3 180 0 Stack Exit Total Particulate OTM - 27/28 3 240 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit



### Saturday, January 22, 2011 Page 3 of 28

### 2010 EGU MACT ICR - CIPCO Fair#2

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.

There were no modifications or deviations to test methods.

Filterable Particulate 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

Inorganic (Aqueous)

Condensible Part. 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

Beryllium Method 29 3 240 0 Stack Exit Arsenic Method 29 3 240 0 Stack Exit Cobalt Method 29 3 240 0 Stack Exit Nickel Method 29 3 240 0 Stack Exit Antimony 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 Filterable Particulate Method 29 3 240 0 Stack Exit Selenium Method 29 3 240 0 Stack Exit O2 Method 3A O2 3 240 0 Stack Exit Co2 Method 3A CO2 3 240 0 Stack Exit Filterable Particulate Method 5/OTM-28 3 240 0 Use only for wet stacks. Delete OTM27/OTM28 test. Stack Exit

Inorganic (Aqueous)

Condensible Part. Method 5/OTM-28 3 240 0 Use only for wet stacks. Delete OTM27/OTM28 test. Stack Exit

Organic Condensible

Particulate Method 5/OTM-28 3 240 0 Use only for wet stacks. Delete OTM27/OTM28 test. Stack Exit

Total Particulate Method 5/OTM-28 3 240 0 Use only for wet stacks. Delete OTM27/OTM28 test. Stack Exit

Filterable Particulate Method 5 3 240 0 Stack Exit Sulfur Dioxide Method 6C 3 180 0 Stack Exit Nitrogen oxides (NOx) Method 7E 3 180 0 Stack Exit



### Saturday, January 22, 2011 Page 4 of 28

### 2010 EGU MACT ICR - CIPCO Fair#2

Sampling / Stack Data Results Summary



### Location Stack Exit - Method 0011 Average
Run Number M0011-1 M0011-2 M0011-3

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

Run Start Time 7:20:00 AM 9:55:00 AM 12:25:00 PM

Run Finish Time 9:27:00 AM 12:07:00 PM 2:32:00 PM

Net Run Time, minutes 120 120 120 Dry Gas Meter Volume Sampled, dscf 90.312 88.405 87.661 88.793
Moisture Content of Stack Gas, % 8.15 8.27 8.53 8.317 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000
Carbon Dioxide, % 13.6 13.4 13.4 13.467 Oxygen, % 5.6 5.7 5.7 5.667 Average Stack Gas Temperature, °F 333.88 340.79 342.83 339.167 Dry Volumetric Flow Rate, dry scfm 106,175.6 103,255.3 102,228.0 103,886.300
Actual Wet Volumetric Flue Gas Flow Rate, acfm 176,042.5 172,916.6 172,120.2 173,693.100 Percent Isokinetic of Sampling Rate, % 96.9 97.5 97.7 97.367
F-Factor, dscfm/MMBtu @ %O2 9499 9567 9736 9,600.667

Fw 0 0 0 0.000

Fc 0 0 0 0.000



### 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



### Saturday, January 22, 2011 Page 5 of 28

### 2010 EGU MACT ICR - CIPCO Fair#2

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



### Saturday, January 22, 2011 Page 6 of 28

### 2010 EGU MACT ICR - CIPCO Fair#2

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



### Saturday, January 22, 2011 Page 7 of 28

### 2010 EGU MACT ICR - CIPCO Fair#2

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



### Saturday, January 22, 2011 Page 8 of 28

### 2010 EGU MACT ICR - CIPCO Fair#2

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



### Saturday, January 22, 2011 Page 9 of 28

### 2010 EGU MACT ICR - CIPCO Fair#2

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 - OTM - 27/28 Average
Run Number

Test Date

Run Start Time

Run Finish Time
Net Run Time, minutes Dry Gas Meter Volume Sampled, dscf
Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, %
Carbon Dioxide, % Oxygen, % Average Stack Gas Temperature, °F Dry Volumetric Flow Rate, dry scfm
Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, %
F-Factor, dscfm/MMBtu @ %O2

Fw

Fc



### Saturday, January 22, 2011 Page 10 of 28

### 2010 EGU MACT ICR - CIPCO Fair#2

Emissions Summary



### Location: Stack Exit - Method 0011 Compound: Formaldehyde Average RunNumber M0011-1 M0011-2 M0011-3 Mass_mg 0.057 0.047 0.009 0.038 lb/mmBtuO2 1.81E-05 1.54E-05 3.03E-06 0.000
ppm 1.79E-02 1.50E-02 2.90E-03 0.012 ppm@7%O2 1.63E-02 1.37E-02 2.65E-03 0.011



### Location: Stack Exit - Method 10 Compound: Carbon Monoxide Average
Run 1 2 3 lb/mmBtuO2 1.11E-02 1.10E-02 1.15E-02 0.011
ppm 1.18E+01 1.15E+01 1.18E+01 11.700 ppm@7%O2 1.07E+01 1.05E+01 1.08E+01 10.667



### Location: Stack Exit - Method 25A Compound: Total organic compounds (TOC) as Average
Run 1 2 3 lb/mmBtuO2 2.49E-03 1.53E-03 2.28E-03 0.002
ppm 1.68E+00 1.02E+00 1.49E+00 1.397 ppm@7%O2 1.53E+00 9.33E-01 1.36E+00 1.274



### Location: Stack Exit - Method 26A Compound: Hydrogen Chloride Average RunNumber M26A-1 M26A-2 M26A-3 Mass_mg 630 620 590 613.333 lb/mmBtuO2 1.86E-01 1.78E-01 1.70E-01 0.178


### Compound: Hydrogen Fluoride Average RunNumber M26A-1 M26A-2 M26A-3 Mass_mg 15 15 19 16.333 lb/mmBtuO2 4.42E-03 4.30E-03 5.48E-03 0.005



### Location: Stack Exit - Method 29 Compound: Antimony Average RunNumber M29-1 M29-2 M29-3 Mass_mg 0.008 0.0147 0.0147 0.012 lb/mmBtuO2 1.32E-06 2.73E-06 2.80E-06 0.000


### Compound: Arsenic Average RunNumber M29-1 M29-2 M29-3 Mass_mg 0.1132 0.2099 0.2254 0.183



### Saturday, January 22, 2011 Page 11 of 28

### 2010 EGU MACT ICR - CIPCO Fair#2

lb/mmBtuO2 1.87E-05 3.89E-05 4.29E-05 0.000


### Compound: Beryllium Average RunNumber M29-1 M29-2 M29-3 Mass_mg 0.00276 0.00684 0.00724 0.006 lb/mmBtuO2 4.56E-07 1.27E-06 1.38E-06 0.000


### Compound: Cadmium Average RunNumber M29-1 M29-2 M29-3 Mass_mg 0.002 0.00264 0.012 0.006 lb/mmBtuO2 3.30E-07 4.90E-07 2.28E-06 0.000


### Compound: Chromium Average RunNumber M29-1 M29-2 M29-3 Mass_mg 0.13093 1.57261 0.45551 0.720 lb/mmBtuO2 2.16E-05 2.92E-04 8.67E-05 0.000


### Compound: Cobalt Average RunNumber M29-1 M29-2 M29-3 Mass_mg 0.00868 0.039 0.0333 0.027 lb/mmBtuO2 1.43E-06 7.23E-06 6.34E-06 0.000


### Compound: Filterable Particulate Average RunNumber M29-1 M29-2 M29-3 Mass_mg 229.3 306.2 375.1 303.533 lb/mmBtuO2 3.79E-02 5.68E-02 7.14E-02 0.055


### Compound: Lead Average RunNumber M29-1 M29-2 M29-3 Mass_mg 0.03252 0.09378 0.10212 0.076 lb/mmBtuO2 5.37E-06 1.74E-05 1.94E-05 0.000


### Compound: Manganese Average RunNumber M29-1 M29-2 M29-3 Mass_mg 0.04216 0.149 0.11846 0.103 lb/mmBtuO2 6.96E-06 2.76E-05 2.25E-05 0.000


### Compound: Nickel Average RunNumber M29-1 M29-2 M29-3 Mass_mg 0.0802 0.9322 0.4039 0.472 lb/mmBtuO2 1.32E-05 1.73E-04 7.69E-05 0.000


### Compound: Selenium Average RunNumber M29-1 M29-2 M29-3 Mass_mg 0.2362 0.2182 0.2282 0.228



### Saturday, January 22, 2011 Page 12 of 28

### 2010 EGU MACT ICR - CIPCO Fair#2

Process Run Data lb/mmBtuO2 3.90E-05 4.05E-05 4.34E-05 0.000



### Location: Stack Exit - OTM - 27/28 Compound: Filterable Particulate Average RunNumber MOTM27/OTM28-1 MOTM27/OTM28-2 MOTM27/OTM28-3 Mass_mg 77.5 495.8 395.2 322.833 lb/mmBtuO2 1.69E-02 1.15E-01 8.90E-02 0.074


### Compound: Filterable PM2.5 Average RunNumber MOTM27/OTM28-1 MOTM27/OTM28-2 MOTM27/OTM28-3 Mass_mg 52.7 304 134.5 163.733 lb/mmBtuO2 1.15E-02 7.08E-02 3.03E-02 0.038


### Compound: Inorganic (Aqueous) Condensible Pa Average RunNumber MOTM27/OTM28-1 MOTM27/OTM28-2 MOTM27/OTM28-3 Mass_mg 288.4 401.2 611.2 433.600 lb/mmBtuO2 6.28E-02 9.34E-02 1.38E-01 0.098


### Compound: Organic Condensible Particulate Average RunNumber MOTM27/OTM28-1 MOTM27/OTM28-2 MOTM27/OTM28-3 Mass_mg 40.6 24.1 8.4 24.367 lb/mmBtuO2 8.84E-03 5.61E-03 1.89E-03 0.005


### Compound: Total Particulate Average RunNumber MOTM27/OTM28-1 MOTM27/OTM28-2 MOTM27/OTM28-3 Mass_mg 406.5 921.1 1014.8 780.800 lb/mmBtuO2 8.85E-02 2.14E-01 2.29E-01 0.177


### Compound: Total PM2.5 Average RunNumber MOTM27/OTM28-1 MOTM27/OTM28-2 MOTM27/OTM28-3 Mass_mg 381.7 729.3 754.1 621.700 lb/mmBtuO2 8.31E-02 1.70E-01 1.70E-01 0.141



### Saturday, January 22, 2011 Page 13 of 28

### 2010 EGU MACT ICR - CIPCO Fair#2

Process Run Data



### Run Name Value UOM Comments Target Value
1 Coal Firing Rate 35800 lb/hr Run 1 - OTM 27/28, M5/29, M30B 36000

1 Average Heat Input 441 MMBtu/hr Run 1 - OTM 27/28, M5/29, M30B 430



### 1 Steam Output 336 1000 lb steam/hr Run 1 - OTM 27/28, M5/29, M30B 330

1 Unit Gross Electrical Output 37.8 MW Run 1 - OTM 27/28, M5/29, M30B 37

2 Coal Firing Rate 37500 lb/hr Run 2 - OTM 27/28, M5/29, M30B 36000

2 Average Heat Input 442 MMBtu/hr Run 2 - OTM 27/28, M5/29, M30B 430



### 2 Steam Output 339 1000 lb steam/hr Run 2 - OTM 27/28, M5/29, M30B 330

2 Unit Gross Electrical Output 37.9 MW Run 2 - OTM 27/28, M5/29, M30B 37

3 Coal Firing Rate 37500 lb/hr Run 3 - OTM 27/28, M5/29, M30B 36000

3 Average Heat Input 440 MMBtu/hr Run 3 - OTM 27/28, M5/29, M30B 430



### 3 Steam Output 334 1000 lb steam/hr Run 3 - OTM 27/28, M5/29, M30B 330

3 Unit Gross Electrical Output 37.5 MW Run 3 - OTM 27/28, M5/29, M30B 37

4 Coal Firing Rate 36400 lb/hr Run 1 - M26A, CTM033 36000

4 Average Heat Input 461 MMBtu/hr Run 1 - M26A, CTM033 430

4 Steam Output 339 1000 lb steam/hr Run 1 - M26A, CTM033 330

4 Unit Gross Electrical Output 37.8 MW Run 1 - M26A, CTM033 37



### Saturday, January 22, 2011 Page 14 of 28

### 2010 EGU MACT ICR - CIPCO Fair#2

5 Coal Firing Rate 39200 lb/hr Run 2 - M26A, CTM033 36000



### 5 Average Heat Input 462 MMBtu/hr Run 2 - M26A, CTM033 430

5 Steam Output 340 1000 lb steam/hr Run 2 - M26A, CTM033 330

5 Unit Gross Electrical Output 37.9 MW Run 2 - M26A, CTM033 37



### 6 Coal Firing Rate 36700 lb/hr Run 3 - M26A, CTM033 36000

6 Average Heat Input 460 MMBtu/hr Run 3 - M26A, CTM033 430



### 6 Steam Output 336 1000 lb steam/hr Run 3 - M26A, CTM033 330

6 Unit Gross Electrical Output 37.6 MW Run 3 - M26A, CTM033 37



### 7 Coal Firing Rate 37100 lb/hr Run 1 - M0010, M0031, M0011, M10, M25/18 36000

7 Average Heat Input 454 MMBtu/hr Run 1 - M0010, M0031, M0011, M10, M25/18 430

7 Steam Output 333 1000 lb steam/hr Run 1 - M0010, M0031, M0011, M10, M25/18 330



### 7 Unit Gross Electrical Output 37.6 MW Run 1 - M0010, M0031, M0011, M10, M25/18 37

8 Coal Firing Rate 37100 lb/hr Run 2 - M0010, M0031, M0011, M10, M25/18 36000

8 Average Heat Input 464 MMBtu/hr Run 2 - M0010, M0031, M0011, M10, M25/18 430

8 Steam Output 335 1000 lb steam/hr Run 2 - M0010, M0031, M0011, M10, M25/18 330

8 Unit Gross Electrical Output 37.7 MW Run 2 - M0010, M0031, M0011, M10, M25/18 37



### 9 Coal Firing Rate 36700 lb/hr Run 3 - M0010, M0031, M0011, M10, M25/18 36000

9 Average Heat Input 464 MMBtu/hr Run 3 - M0010, M0031, M0011, M10, M25/18 430



### Saturday, January 22, 2011 Page 15 of 28

### 2010 EGU MACT ICR - CIPCO Fair#2

APCD Run Data

Process Lab Run Data 9 Steam Output 335 1000 lb steam/hr Run 3 - M0010, M0031, M0011, M10, M25/18 330

9 Unit Gross Electrical Output 37.7 MW Run 3 - M0010, M0031, M0011, M10, M25/18 37

Run Name Value UOM Comments Target Value
LOW NOX BURNERS lb/mmBTU 0.46

ELECTROSTATIC PRECIPITATOR lb/mmBTU 0.43

Run Name Value UOM Comments


### 1 See Comments. 0

Saturday, January 22, 2011 Page 16 of 28

### 2010 EGU MACT ICR - CIPCO Fair#2

Sampling / Stack Data Results Detail



### Location Stack Exit - Method 0011 Average Run Number M0011-1 M0011-2 M0011-3
Test Date 8/6/2010 8/6/2010 8/6/2010 Run Start Time 7:20:00 AM 9:55:00 AM 12:25:00 PM Run Finish Time 9:27:00 AM 12:07:00 PM 2:32:00 PM Net Traversing Points 28 28 28 Net Run Time, minutes 120 120 120 Nozzle Diameter, inches 0.211 0.211 0.211 0.211 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 1.003 1.003 1.003 1.003 Barometric Pressure, inches of Mercury 29.5 29.5 29.5 29.500 Average Orifice Meter Differential, inches H2O 1.63 1.53 1.54 1.567 Dry Gas Meter Volume Sampled, cubic feet 92.620 92.500 91.540 92.220 Average Dry Gas Meter Temperature, °F 77.67 88.42 87.35 84.480 Dry Gas Meter Volume Sampled, dscf 90.312 88.405 87.661 88.793 Total Moisture Liquid collected, g 170.1 169.3 173.5 170.967 Volume of Water Vapor, standard cubic feet 8.01 7.97 8.17 8.050 Moisture Content of Stack Gas, % 8.15 8.27 8.53 8.317 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9185 0.9173 0.9147 0.917 Carbon Dioxide, % 13.6 13.4 13.4 13.467 Oxygen, % 5.6 5.7 5.7 5.667 Carbon Monoxide & Nitrogen, % 80.8 80.9 80.9 80.867 Fuel Factor 1.13 1.13 1.13 Dry Molecular Weight, lb/lb-Mole 30.40 30.37 30.37 30.380 Wet Molecular weight, lb/lb-Mole 29.39 29.35 29.31 29.350 Flue Gas Static Pressure, inches of H2O 0.5 0.5 0.5 0.500 Absolute Flue Gas Pressure, inches of Mercury 29.54 29.54 29.54 29.540 Average Stack Gas Temperature, °F 333.88 340.79 342.83 339.167 Average Velocity Head, inches of H2O 1.6578904574 2867 1.583712666

25913 1.562967744

07957 1.602

Average Stack Gas Velocity, feet/second 88.42 86.85 86.45 87.240 Stack Cross-Sectional Area, square feet 33.183 33.183 33.183 33.183 Dry Volumetric Flow Rate, dry scfm 106,175.6 103,255.3 102,228.0 103,886.300 Actual Wet Volumetric Flue Gas Flow Rate, acfm 176,042.5 172,916.6 172,120.2 173,693.100 Percent Isokinetic of Sampling Rate, % 96.9 97.5 97.7 97.367 Percent Excess Air, % 35.6 36.4 36.4 36.133 F-Factor, dscfm/MMBtu @ %O2 9499 9567 9736 9,600.667 Round Duct Diameter, inches 78 78 78 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0
Fw 0 0 0 0.000
Fc 0 0 0 0.000



### Saturday, January 22, 2011 Page 17 of 28

### 2010 EGU MACT ICR - CIPCO Fair#2

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



### Saturday, January 22, 2011 Page 18 of 28

### 2010 EGU MACT ICR - CIPCO Fair#2

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



### Saturday, January 22, 2011 Page 19 of 28

### 2010 EGU MACT ICR - CIPCO Fair#2

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
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### Saturday, January 22, 2011 Page 20 of 28

### 2010 EGU MACT ICR - CIPCO Fair#2

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
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### Saturday, January 22, 2011 Page 21 of 28

### 2010 EGU MACT ICR - CIPCO Fair#2

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



### Saturday, January 22, 2011 Page 22 of 28

### 2010 EGU MACT ICR - CIPCO Fair#2

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



### Saturday, January 22, 2011 Page 23 of 28

### 2010 EGU MACT ICR - CIPCO Fair#2

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



### Saturday, January 22, 2011 Page 24 of 28

### 2010 EGU MACT ICR - CIPCO Fair#2

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



### Saturday, January 22, 2011 Page 25 of 28

### 2010 EGU MACT ICR - CIPCO Fair#2

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



### Saturday, January 22, 2011 Page 26 of 28

### 2010 EGU MACT ICR - CIPCO Fair#2

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



### Saturday, January 22, 2011 Page 27 of 28

### 2010 EGU MACT ICR - CIPCO Fair#2

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
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### Saturday, January 22, 2011 Page 28 of 28