Name: Mechael L Menne

Title: VP Environmental Safety/Health

Company: Ameren Services

Sign Date: 9/7/2010

Name: Bill Ansell

Title: Program Manager

Company: Clean Air Engineering, Inc.

Sign Date: 9/7/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Newton Unit 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.

Tuesday, January 18, 2011 Page 1 of 18
Newton Unit 2

9/7/2010

Facility Information:

Newton

6725 N. 500th St.

Newton IL 62448

Contact: Donald Schuh

Phone: 314-554-2658

Fax: 314-554-4182

Email: dschuh@ameren.com

Testing Company:

Clean Air Engineering

500 West Wood Street

Palatine IL 60067

Contact:Bill Ansell

Phone: 847-654-4545

Fax: 847-991-3385

Email: bansell@cleanair.com

Air Permit Number:

6017

Permitted Source ID/Name:

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

Permitted Maximum Process Rate:

N/A

Max. Normal Operation Process Rate:

N/A

Target Process Test Rate

N/A

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

 process flow diagram:

Newton Unit 2 is a tangentially-fired boiler nominally rated at 5,500 million Btu per hour (MMBtu/hr), which entered 

service in 1982. The boiler supplies steam to a steam turbine with a rated gross electrical generating capacity of 638 

MW. The boiler fires pulverized sub-bituminous coals.

Unit 2 is equipped with low-NOX burners and an electrostatic precipitator (ESP) to control emissions. An SO3 

injection system is used to condition flue gas to improve the efficiency of the ESP. An activated carbon injection 

(ACI) system is installed upstream of the ESP to control mercury emissions.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 1707900011 FRS #: 110000439393

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 316.26 0 0 0 2 10.1 4 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Exit Carbon Monoxide Method 10 3 120 0

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 3 120 0

Stack Exit Hydrogen Fluoride Method 26A 3 60 0

Tuesday, January 18, 2011 Page 2 of 18
Newton Unit 2

9/7/2010

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

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

of request AND approval, including dates.

Oxygen (O2) and carbon dioxide (CO2) data (units of dry volume percent, %dv) used in molecular weight 

calculations, O2 correction and calculation of Fd-based emissions (units of lb/MMBtu) were obtained in the 

following manner during the test program:

•	For non-instrumental (wet) sampling methods, a modified version of EPA Method 3B was utilized. 

o	Multi-point, integrated gas samples (IGS) were continuously collected at a constant rate from a slipstream of the 

exhaust of the sample trains into a flexible vinyl bag (IGS bag), per Method 3B specifications. 

o	A calibrated paramagnetic/IR analyzer was used in place of a traditional Orsat analyzer to measure drift-corrected 

O2 and CO2 concentrations of the IGS bags, per Method 3A specifications.

o	Multiple IGS bags were collected during lengthy sample runs to ensure sample train integrity. Average O2 and CO2 

results for each test run were calculated.

Stack Exit Hydrogen Chloride Method 26A 3 60 0

Total PM2.5 OTM - 27/28 3 360 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Organic Condensible 

Particulate

OTM - 27/28 3 360 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Inorganic (Aqueous) 

Condensible Part.

OTM - 27/28 3 360 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Filterable PM2.5 OTM - 27/28 3 360 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Stack Exit Filterable Particulate 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 Manganese Method 29 3 240 0

Stack Exit Selenium Method 29 3 240 0

Stack Exit Cobalt Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Tuesday, January 18, 2011 Page 3 of 18
Newton Unit 2

9/7/2010

Sampling / Stack Data Results Summary

Location Stack Exit - Method 10

Average

Run Number 1 2 3

Test Date 6/17/2010 6/18/2010 6/18/2010

Run Start Time 2:11:00 PM 11:28:00 

AM

4:46:00 PM

Run Finish Time 4:36:00 PM 2:16:00 PM 7:50:00 PM

Carbon Dioxide, % 14.4 15.3 15.3 15.000

Oxygen, % 5 4.1 4.1 4.400

Dry Volumetric Flow Rate, dry scfm 1602432 1557236 1569291 1,576,319.66

7

F-Factor, dscfm/MMBtu @ %O2 9613 9604 9604 9,607.000

Moisture, % 8.6 13.8 13.3 11.900

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Stack Exit - Method 25A

Average

Run Number 1 2 3

Test Date 6/17/2010 6/18/2010 6/18/2010

Run Start Time 2:11:00 PM 11:28:00 

AM

4:46:00 PM

Run Finish Time 4:36:00 PM 2:16:00 PM 7:50:00 PM

Carbon Dioxide, % 14.4 15.3 15.3 15.000

Oxygen, % 5 4.1 4.1 4.400

Dry Volumetric Flow Rate, dry scfm 1602432 1557236 1569291 1,576,319.66

7

F-Factor, dscfm/MMBtu @ %O2 9613 9604 9604 9,607.000

Moisture, % 8.6 13.8 13.3 11.900

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, January 18, 2011 Page 4 of 18
Newton Unit 2

9/7/2010

Location Stack Exit - Method 26A

Average

Run Number M26A-1 M26A-2 M26A-3

Test Date 6/16/2010 6/22/2010 6/22/2010

Run Start Time 4:24:00 PM 11:57:00 

AM

2:31:00 PM

Run Finish Time 5:19:00 PM 12:52:00 

PM

3:26:00 PM

Net Run Time, minutes 60 60 60

Dry Gas Meter Volume Sampled, dscf 36.025 35.691 36.185 35.967

Moisture Content of Stack Gas, % 13.31 14.10 14.32 13.910

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

Carbon Dioxide, % 14 14.5 14.1 14.200

Oxygen, % 5.4 4.1 4.4 4.633

Average Stack Gas Temperature, °F 357.17 359.25 354.75 357.057

Dry Volumetric Flow Rate, dry scfm 1,382,895.7 1,354,318.4 1,364,489.0 1,367,234.36

7

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,541,937.6 2,518,698.2 2,530,154.2 2,530,263.33

3

Percent Isokinetic of Sampling Rate, % 98.5 99.6 100.2 99.433

F-Factor, dscfm/MMBtu @ %O2 9836 9683 9623 9,714.000

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, January 18, 2011 Page 5 of 18
Newton Unit 2

9/7/2010

Location Stack Exit - Method 29

Average

Run Number M5/29-1 M5/29-2 M5/29-4

Test Date 6/16/2010 6/17/2010 6/22/2010

Run Start Time 7:05:00 AM 7:22:00 

AM

11:57:00 AM

Run Finish Time 11:00:00 AM 11:17:00 

AM

3:52:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 134.564 138.994 131.766 135.108

Moisture Content of Stack Gas, % 13.62 13.69 13.87 13.727

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

Carbon Dioxide, % 14 13.9 14.8 14.233

Oxygen, % 5.2 4.8 4.5 4.833

Average Stack Gas Temperature, °F 348.08 341.23 355.50 348.270

Dry Volumetric Flow Rate, dry scfm 1,312,528.1 1,311,104.4 1,273,243.1 1,298,958.53

3

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,394,318.0 2,373,369.8 2,350,784.9 2,372,824.23

3

Percent Isokinetic of Sampling Rate, % 96.9 100.2 97.8 98.300

F-Factor, dscfm/MMBtu @ %O2 9816 9613 9639 9,689.333

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, January 18, 2011 Page 6 of 18
Newton Unit 2

9/7/2010

Location Stack Exit - OTM - 27/28

Average

Run Number M027/028-1 M027/028-

2

M027/028-3

Test Date 6/16/2010 6/17/2010 6/18/2010

Run Start Time 8:17:00 AM 7:22:00 

AM

7:44:00 AM

Run Finish Time 2:17:48 PM 1:12:54 PM 1:24:18 PM

Net Run Time, minutes 368.3 358.1 347.5

Dry Gas Meter Volume Sampled, dscf 116.096 116.628 110.277 114.334

Moisture Content of Stack Gas, % 12.90 13.17 13.88 13.317

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

Carbon Dioxide, % 13 13.8 14.3 13.700

Oxygen, % 5.9 5 4.5 5.133

Average Stack Gas Temperature, °F 351.38 347.69 350.88 349.983

Dry Volumetric Flow Rate, dry scfm 1,374,484.9 1,386,950.4 1,334,543.4 1,365,326.23

3

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,496,768.0 2,515,752.3 2,450,289.1 2,487,603.13

3

Percent Isokinetic of Sampling Rate, % 85.3 87.3 88.4 87.000

F-Factor, dscfm/MMBtu @ %O2 9816 9638 9377 9,610.333

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, January 18, 2011 Page 7 of 18
Newton Unit 2

9/7/2010

Emissions Summary

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 3.86E-01 4.23E-01 4.53E-01 0.421

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 3.29E-04 5.45E-04 9.01E-04 0.001

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber M26A-1 M26A-2 M26A-3

Mass_mg 0.77 0.521 0.604 0.632

lb/mmBtuO2 6.25E-04 3.88E-04 4.49E-04 0.000

Compound: Hydrogen Fluoride

Average

RunNumber M26A-1 M26A-2 M26A-3

Mass_mg 5.314 3.535 4.292 4.380

lb/mmBtuO2 4.31E-03 2.63E-03 3.19E-03 0.003

Location: Stack Exit - Method 29

Compound: Antimony

Average

RunNumber M5/29-1 M5/29-2 M5/29-4

Mass_mg 0.000438 0.0009186 0.000861 0.001

lb/mmBtuO2 9.38E-08 1.82E-07 1.77E-07 0.000

Compound: Arsenic

Average

RunNumber M5/29-1 M5/29-2 M5/29-4

Mass_mg 0.010804 0.0104778 0.0112947 0.011

lb/mmBtuO2 2.31E-06 2.07E-06 2.32E-06 0.000

Compound: Beryllium

Average

RunNumber M5/29-1 M5/29-2 M5/29-4

Mass_mg 0.0002379 0.000206 0.0002187 0.000

lb/mmBtuO2 5.09E-08 4.08E-08 4.49E-08 0.000

Compound: Cadmium

Average

RunNumber M5/29-1 M5/29-2 M5/29-4

Mass_mg 0.0006878 0.0007118 0.0006274 0.001

lb/mmBtuO2 1.47E-07 1.41E-07 1.29E-07 0.000

Tuesday, January 18, 2011 Page 8 of 18
Newton Unit 2

9/7/2010

Compound: Chromium

Average

RunNumber M5/29-1 M5/29-2 M5/29-4

Mass_mg 0.0060964 0.007706 0.0058955 0.007

lb/mmBtuO2 1.31E-06 1.53E-06 1.21E-06 0.000

Compound: Cobalt

Average

RunNumber M5/29-1 M5/29-2 M5/29-4

Mass_mg 0.0017906 0.0014827 0.003192 0.002

lb/mmBtuO2 3.83E-07 2.93E-07 6.56E-07 0.000

Compound: Filterable Particulate

Average

RunNumber M5/29-1 M5/29-2 M5/29-4

Mass_mg 43.16 43.23 46.47 44.287

lb/mmBtuO2 9.24E-03 8.56E-03 9.55E-03 0.009

Compound: Lead

Average

RunNumber M5/29-1 M5/29-2 M5/29-4

Mass_mg 0.0034009 0.0026884 0.0036005 0.003

lb/mmBtuO2 7.28E-07 5.32E-07 7.40E-07 0.000

Compound: Manganese

Average

RunNumber M5/29-1 M5/29-2 M5/29-4

Mass_mg 0.0101684 0.0095647 0.012185 0.011

lb/mmBtuO2 2.18E-06 1.89E-06 2.50E-06 0.000

Compound: Nickel

Average

RunNumber M5/29-1 M5/29-2 M5/29-4

Mass_mg 0.0057434 0.0111566 0.0047281 0.007

lb/mmBtuO2 1.23E-06 2.21E-06 9.72E-07 0.000

Compound: Selenium

Average

RunNumber M5/29-1 M5/29-2 M5/29-4

Mass_mg 0.1057552 0.1086825 0.1113582 0.109

lb/mmBtuO2 2.26E-05 2.15E-05 2.29E-05 0.000

Location: Stack Exit - OTM - 27/28

Compound: Filterable PM2.5

Average

RunNumber M027/028-1 M027/028-2 M027/028-3

Mass_mg 23.26 25.91 21.94 23.703

lb/mmBtuO2 6.04E-03 6.20E-03 5.24E-03 0.006

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber M027/028-1 M027/028-2 M027/028-3

Mass_mg 24.32 22.08 21.12 22.507

Tuesday, January 18, 2011 Page 9 of 18
Newton Unit 2

9/7/2010

Process Run Data

lb/mmBtuO2 6.32E-03 5.29E-03 5.05E-03 0.006

Compound: Organic Condensible Particulate

Average

RunNumber M027/028-1 M027/028-2 M027/028-3

Mass_mg 2.71 2.41 2.02 2.380

lb/mmBtuO2 7.04E-04 5.77E-04 4.83E-04 0.001

Compound: Total PM2.5

Average

RunNumber M027/028-1 M027/028-2 M027/028-3

Mass_mg 50.29 50.4 45.08 48.590

lb/mmBtuO2 1.31E-02 1.21E-02 1.08E-02 0.012

Tuesday, January 18, 2011 Page 10 of 18
Newton Unit 2

9/7/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Coal Firing Rate 352.96 klb/hr 0

2 Coal Firing Rate 352.96 klb/hr 0

3 Coal Firing Rate 357.71 klb/hr 0

1 Average Heat Input 5666 MMBtu/hr 0

2 Average Heat Input 5760 MMBtu/hr 0

3 Average Heat Input 5792 MMBtu/hr 0

1 Steam Output 4115.6 1000 lb steam/hr 0

2 Steam Output 4041.5 1000 lb steam/hr 0

3 Steam Output 4114.5 1000 lb steam/hr 0

1 Synfuel Firing Rate 0 0

2 Synfuel Firing Rate 0 0

3 Synfuel Firing Rate 0 0

1 Petroleum Coke Firing Rate 0 0

2 Petroleum Coke Firing Rate 0 0

3 Petroleum Coke Firing Rate 0 0

1 Coal Gas Firing Rate 0 0

2 Coal Gas Firing Rate 0 0

3 Coal Gas Firing Rate 0 0

1 Fuel Oil Firing Rate 0 0

2 Fuel Oil Firing Rate 0 0

3 Fuel Oil Firing Rate 0 0

1 Flue Gas Flow Rate 0 scfh 0

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

1 FGD Scrubber Liquor pH 0 pH 0

1 FGD Scrubber Liquor Flow Rate 0 gal/min 0

1 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

1 Flue Gas Oxygen Content 0 % 0

1 Flue Gas Carbon Dioxide Content 0 % 0

1 Flue Gas Moisture Content 0 % 0

1 Flue Gas Sampling Point Temperature 0 Deg F 0

1 Flue Gas Pressure 0 atm 0

1 Standard Pressure 0 atm 0

1 Standard Temperature 0 Deg F 0

Tuesday, January 18, 2011 Page 11 of 18
Newton Unit 2

9/7/2010

APCD Run Data

Process Lab Run Data

1 Unit Gross Electrical Output 616.86 MW 0

1 Unit Net Electric Generation 587.13 MWh 0

Run Name Value UOM Comments

Target

Value

1 LOW NOX BURNERS 0 0

1 OVERFIRE AIR 0 0

1 ACTIVATED CARBON ADSORPTION 0 0

1 ELECTROSTATIC PRECIPITATOR 0 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value 11852 Btu/lb

1 Fuel Moisture 30.28 %

1 Fuel Mercury Content 0.228 ppm

1 Fuel Cadmium Content 0.095 ppm

1 Ultimate/Proximate Analysis 0

1 Fuel Nickel Content 5.96 ppm

1 Fuel Arsenic Content 1.7 ppm

1 Fuel Chromium Content 5.99 ppm

1 Fuel Beryllium Content 0.315 ppm

1 Fuel Lead Content 2.82 ppm

1 Fuel Manganese Content 12.8 ppm

1 Fuel Chlorine Content 0.002 %

1 Fuel Fluorine Content 74.1 ppm

2 Fuel Higher Heating Value 11984 Btu/lb

2 Fuel Moisture 30.36 %

2 Fuel Mercury Content 0.174 ppm

2 Fuel Cadmium Content 0.099 ppm

2 Ultimate/Proximate Analysis 0

2 Fuel Nickel Content 5.55 ppm

2 Fuel Arsenic Content 1.43 ppm

2 Fuel Chromium Content 5.12 ppm

2 Fuel Beryllium Content 0.256 ppm

2 Fuel Lead Content 3.18 ppm

2 Fuel Manganese Content 15 ppm

2 Fuel Chlorine Content 0.004 %

2 Fuel Fluorine Content 73.7 ppm

3 Fuel Higher Heating Value 11992 Btu/lb

3 Fuel Moisture 28.29 %

Tuesday, January 18, 2011 Page 12 of 18
Newton Unit 2

9/7/2010

3 Fuel Mercury Content 0.131 ppm

3 Fuel Cadmium Content 0.070 ppm

3 Ultimate/Proximate Analysis 0

3 Fuel Nickel Content 4.03 ppm

3 Fuel Arsenic Content 1.07 ppm

3 Fuel Chromium Content 4.33 ppm

3 Fuel Beryllium Content 0.187 ppm

3 Fuel Lead Content 2.11 ppm

3 Fuel Manganese Content 10.8 ppm

3 Fuel Chlorine Content 0.002 %

3 Fuel Fluorine Content 69.6 ppm

Tuesday, January 18, 2011 Page 13 of 18
Newton Unit 2

9/7/2010

Sampling / Stack Data Results Detail

Location Stack Exit - Method 10

Average

Run Number 1 2 3

Test Date 6/17/2010 6/18/2010 6/18/2010

Run Start Time 2:11:00 PM 11:28:00 AM 4:46:00 PM

Run Finish Time 4:36:00 PM 2:16:00 PM 7:50:00 PM

Carbon Dioxide, % 14.4 15.3 15.3 15.000

Oxygen, % 5 4.1 4.1 4.400

Fuel Factor 1.1 0 1.1

Dry Volumetric Flow Rate, dry scfm 1602432 1557236 1569291 1,576,319.6

67

F-Factor, dscfm/MMBtu @ %O2 9613 9604 9604 9,607.000

Moisture, % 8.6 13.8 13.3 11.900

Analyzer Make T.E.I T.E.I T.E.I

Analyzer Model 48CHL 48CHL 48CHL

Analyzer Serial Number 204765 204765 204765 204,765.000

Operating Range 1000 1000 1000 1,000.000

Operating Units PPM PPM PPM

No. Readings/Avg. 60 60 60 60.000

Calibration Set 1 2 2 1.667

Calibration Pre Zero Cylinder ID ALM004086 ALM004086 ALM004086

Calibration Pre Zero Cylinder Instrument Response 0 0 0.054 0.018

Calibration Pre Zero Cylinder Bias 0.03 0 0.06 0.030

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID ALM036995 ALM036995 ALM036995

Calibration Pre High Cylinder Instrument Response 247.972 242.567 242.019 244.186

Calibration Pre High Cylinder Bias -0.02 -0.36 -0.43 -0.270

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID ALM004086 ALM004086 ALM004086

Calibration Post Zero Cylinder Instrument Response 0.081 0.054 -0.033 0.034

Calibration Post Zero Cylinder Bias 0.04 0.06 0.05 0.050

Calibration Post Zero Cylinder Drift 0.01 0.06 0.01 0.027

Calibration Post High Cylinder ID ALM036995 ALM036995 ALM036995

Calibration Post High Cylinder Instrument Response 245.595 242.019 231.746 239.787

Calibration Post High Cylinder Bias -0.32 -0.43 -1.73 -0.827

Calibration Post High Cylinder Drift 0.3 0.07 1.3 0.557

Cavg 417.101 475.423 497.05 463.191

Cavg Units ppmvd ppmvd ppmvd

Cgas 419.8613 487.4327 521.2292 476.174

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Cgasw 0 0 0 0.000

Cgasw Units

Tuesday, January 18, 2011 Page 14 of 18
Newton Unit 2

9/7/2010

Location Stack Exit - Method 25A

Average

Run Number 1 2 3

Test Date 6/17/2010 6/18/2010 6/18/2010

Run Start Time 2:11:00 PM 11:28:00 AM 4:46:00 PM

Run Finish Time 4:36:00 PM 2:16:00 PM 7:50:00 PM

Carbon Dioxide, % 14.4 15.3 15.3 15.000

Oxygen, % 5 4.1 4.1 4.400

Fuel Factor 1.1 1.1 1.1

Dry Volumetric Flow Rate, dry scfm 1602432 1557236 1569291 1,576,319.6

67

F-Factor, dscfm/MMBtu @ %O2 9613 9604 9604 9,607.000

Moisture, % 8.6 13.8 13.3 11.900

Analyzer Make T.E.I. T.E.I. T.E.I.

Analyzer Model 55C 55C 55C

Analyzer Serial Number 207021 207021 207021 207,021.000

Operating Range 100 100 100 100.000

Operating Units PPM PPM PPM

No. Readings/Avg. 60 60 60 60.000

Calibration Set 3 4 4 3.667

Calibration Pre Zero Cylinder ID ALM004086 ALM004086 ALM004086

Calibration Pre Zero Cylinder Instrument Response 0.307 0.344 0.307 0.319

Calibration Pre Zero Cylinder Bias 0 -0.05 -0.12 -0.057

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID ALM016620 ALM016620 ALM016620

Calibration Pre High Cylinder Instrument Response 24.447 24.058 23.957 24.154

Calibration Pre High Cylinder Bias -0.14 -1.17 -1.38 -0.897

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID ALM004086 ALM004086 ALM004086

Calibration Post Zero Cylinder Instrument Response 0.3 0.307 0.307 0.305

Calibration Post Zero Cylinder Bias -0.01 -0.12 -0.12 -0.083

Calibration Post Zero Cylinder Drift 0.01 0.07 0 0.027

Calibration Post High Cylinder ID ALM016620 ALM016620 ALM016620

Calibration Post High Cylinder Instrument Response 23.384 23.957 22.798 23.380

Calibration Post High Cylinder Bias -2.27 -1.38 -3.7 -2.450

Calibration Post High Cylinder Drift 2.13 0.21 2.32 1.553

Cavg 0.5 0.703 0.834 0.679

Cavg Units ppmvw ppmvd ppmvw

Cgas 0.2276 0.3985 0.6587 0.428

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Cgasw 0.2080509910

21514

0 0.571075616

046466

0.260

Cgasw Units ppmvw ppmvw

Tuesday, January 18, 2011 Page 15 of 18
Newton Unit 2

9/7/2010

Location Stack Exit - Method 26A

Average

Run Number M26A-1 M26A-2 M26A-3

Test Date 6/16/2010 6/22/2010 6/22/2010

Run Start Time 4:24:00 PM 11:57:00 AM 2:31:00 PM

Run Finish Time 5:19:00 PM 12:52:00 PM 3:26:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 60 60 60

Nozzle Diameter, inches 0.21 0.21 0.21 0.210

Pitot Tube Coefficient 0.832 0.832 0.832 0.832

Dry Gas Meter Calibration Factor 0.9898 0.9901 0.9901 0.990

Barometric Pressure, inches of Mercury 29.1 29.1 29.1 29.100

Average Orifice Meter Differential, inches H2O 1.32 1.37 1.38 1.357

Dry Gas Meter Volume Sampled, cubic feet 39.255 38.690 38.575 38.840

Average Dry Gas Meter Temperature, °F 95.71 93.08 83.92 90.903

Dry Gas Meter Volume Sampled, dscf 36.025 35.691 36.185 35.967

Total Moisture Liquid collected, g 117.4 124.5 128.5 123.467

Volume of Water Vapor, standard cubic feet 5.53 5.86 6.05 5.813

Moisture Content of Stack Gas, % 13.31 14.10 14.32 13.910

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

Dry Mole Fraction 0.8669 0.859 0.8568 0.861

Carbon Dioxide, % 14 14.5 14.1 14.200

Oxygen, % 5.4 4.1 4.4 4.633

Carbon Monoxide & Nitrogen, % 80.6 81.4 81.5 81.167

Fuel Factor 1.11 1.16 1.17

Dry Molecular Weight, lb/lb-Mole 30.46 30.48 30.43 30.457

Wet Molecular weight, lb/lb-Mole 28.80 28.72 28.65 28.723

Flue Gas Static Pressure, inches of H2O -0.6 -0.6 -0.6 -0.600

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

Average Stack Gas Temperature, °F 357.17 359.25 354.75 357.057

Average Velocity Head, inches of H2O 1.2209826333

8906

1.192313852

27343

1.206784247

68179

1.207

Average Stack Gas Velocity, feet/second 77.66 76.95 77.30 77.303

Stack Cross-Sectional Area, square feet 545.527 545.527 545.527 545.527

Dry Volumetric Flow Rate, dry scfm 1,382,895.7 1,354,318.4 1,364,489.0 1,367,234.3

67

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,541,937.6 2,518,698.2 2,530,154.2 2,530,263.3

33

Percent Isokinetic of Sampling Rate, % 98.5 99.6 100.2 99.433

Percent Excess Air, % 34.0 23.6 25.7 27.767

F-Factor, dscfm/MMBtu @ %O2 9836 9683 9623 9,714.000

Round Duct Diameter, inches 316.26 316.26 316.26

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

Tuesday, January 18, 2011 Page 16 of 18
Newton Unit 2

9/7/2010

Location Stack Exit - Method 29

Average

Run Number M5/29-1 M5/29-2 M5/29-4

Test Date 6/16/2010 6/17/2010 6/22/2010

Run Start Time 7:05:00 AM 7:22:00 AM 11:57:00 AM

Run Finish Time 11:00:00 AM 11:17:00 AM 3:52:00 PM

Net Traversing Points 48 48 48

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.21 0.21 0.21 0.210

Pitot Tube Coefficient 0.82 0.82 0.82 0.820

Dry Gas Meter Calibration Factor 0.9892 0.9892 0.9898 0.989

Barometric Pressure, inches of Mercury 29.1 29.1 29.1 29.100

Average Orifice Meter Differential, inches H2O 1.14 1.22 1.09 1.150

Dry Gas Meter Volume Sampled, cubic feet 142.515 149.275 141.760 144.517

Average Dry Gas Meter Temperature, °F 79.55 87.24 88.35 85.047

Dry Gas Meter Volume Sampled, dscf 134.564 138.994 131.766 135.108

Total Moisture Liquid collected, g 450.7 468.3 450.9 456.633

Volume of Water Vapor, standard cubic feet 21.21 22.04 21.22 21.490

Moisture Content of Stack Gas, % 13.62 13.69 13.87 13.727

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

Dry Mole Fraction 0.8638 0.8631 0.8613 0.863

Carbon Dioxide, % 14 13.9 14.8 14.233

Oxygen, % 5.2 4.8 4.5 4.833

Carbon Monoxide & Nitrogen, % 80.8 81.3 80.7 80.933

Fuel Factor 1.12 1.16 1.11

Dry Molecular Weight, lb/lb-Mole 30.45 30.42 30.55 30.473

Wet Molecular weight, lb/lb-Mole 28.75 28.72 28.81 28.760

Flue Gas Static Pressure, inches of H2O -0.6 -0.6 -0.6 -0.600

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

Average Stack Gas Temperature, °F 348.08 341.23 355.50 348.270

Average Velocity Head, inches of H2O 1.1258034367

0895

1.114333819

32991

1.077666265

34709

1.106

Average Stack Gas Velocity, feet/second 73.15 72.51 71.82 72.493

Stack Cross-Sectional Area, square feet 545.527 545.527 545.527 545.527

Dry Volumetric Flow Rate, dry scfm 1,312,528.1 1,311,104.4 1,273,243.1 1,298,958.5

33

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,394,318.0 2,373,369.8 2,350,784.9 2,372,824.2

33

Percent Isokinetic of Sampling Rate, % 96.9 100.2 97.8 98.300

Percent Excess Air, % 32.2 28.8 26.8 29.267

F-Factor, dscfm/MMBtu @ %O2 9816 9613 9639 9,689.333

Round Duct Diameter, inches 316.26 316.26 316.26

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

Tuesday, January 18, 2011 Page 17 of 18
Newton Unit 2

9/7/2010

Location Stack Exit - OTM - 27/28

Average

Run Number M027/028-1 M027/028-2 M027/028-3

Test Date 6/16/2010 6/17/2010 6/18/2010

Run Start Time 8:17:00 AM 7:22:00 AM 7:44:00 AM

Run Finish Time 2:17:48 PM 1:12:54 PM 1:24:18 PM

Net Traversing Points 48 48 48

Net Run Time, minutes 368.3 358.1 347.5

Nozzle Diameter, inches 0.164 0.164 0.164 0.164

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9901 0.9901 0.9901 0.990

Barometric Pressure, inches of Mercury 29.1 29.1 29.1 29.100

Average Orifice Meter Differential, inches H2O 0.40 0.40 0.40 0.400

Dry Gas Meter Volume Sampled, cubic feet 124.509 123.982 119.444 122.645

Average Dry Gas Meter Temperature, °F 85.84 81.05 91.27 86.053

Dry Gas Meter Volume Sampled, dscf 116.096 116.628 110.277 114.334

Total Moisture Liquid collected, g 365.4 375.9 377.7 373.000

Volume of Water Vapor, standard cubic feet 17.20 17.69 17.78 17.557

Moisture Content of Stack Gas, % 12.90 13.17 13.88 13.317

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

Dry Mole Fraction 0.871 0.8683 0.8612 0.867

Carbon Dioxide, % 13 13.8 14.3 13.700

Oxygen, % 5.9 5 4.5 5.133

Carbon Monoxide & Nitrogen, % 81.1 81.2 81.2 81.167

Fuel Factor 1.15 1.15 1.15

Dry Molecular Weight, lb/lb-Mole 30.32 30.41 30.47 30.400

Wet Molecular weight, lb/lb-Mole 28.73 28.78 28.74 28.750

Flue Gas Static Pressure, inches of H2O -0.6 -0.6 -0.6 -0.600

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

Average Stack Gas Temperature, °F 351.38 347.69 350.88 349.983

Average Velocity Head, inches of H2O 1.1609971750

4623

1.186159892

88625

1.119286801

06095

1.155

Average Stack Gas Velocity, feet/second 76.28 76.86 74.86 76.000

Stack Cross-Sectional Area, square feet 545.527 545.527 545.527 545.527

Dry Volumetric Flow Rate, dry scfm 1,374,484.9 1,386,950.4 1,334,543.4 1,365,326.2

33

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,496,768.0 2,515,752.3 2,450,289.1 2,487,603.1

33

Percent Isokinetic of Sampling Rate, % 85.3 87.3 88.4 87.000

Percent Excess Air, % 38.0 30.4 26.6 31.667

F-Factor, dscfm/MMBtu @ %O2 9816 9638 9377 9,610.333

Round Duct Diameter, inches 316.26 316.26 316.26

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

Tuesday, January 18, 2011 Page 18 of 18