Name:

Title:

Company:

Sign Date:

Name:

Title:

Company:

Sign Date:

Permitted Facility Representative / Date Testing Company Representative / Date

KCP&L GMO Sibley Units 1, 2, and 3 ICR Testing

Final Test Report 

for

/ /

Based on information and belief formed 

after reasonable inquiry, I certify that the 

statements and information in this test 

report are true, accurate, and complete.

I have reviewed all testing details and 

results in this test report and hereby 

certify that the test report is authentic 

and accurate.

Wednesday, February 16, 2011 Page 1 of 13
KCP&L GMO Sibley Units 1, 2, and 3 ICR Testing

Facility Information:

KCP&L GMO Sibley Generating Station

33200 E Johnson Rd.

Sibley MO 64088

Contact: Steve Brooks

Phone: (816) 650-2931

Fax:

Email: Steve.Brooks@kcpl.com

Testing Company:

Civil & Environmental Consultants, Inc.

4848 Park 370 Blvd. Suite F

Hazelwood MO 63042

Contact: Frank Stevens

Phone: (314) 656-4566

Fax: (314) 656-4595

Email: fstevens@cecinc.com

Air Permit Number:

2094

Permitted Source ID/Name:

095-0031 Sibley Generating Station

Permitted Maximum Process Rate: Max. Normal Operation Process Rate: Target Process Test Rate

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

 process flow diagram:

Sibley Generating Station consists of three (3) Babcock & Wilcox cyclone boilers which are ducted to a common 

stack. Boiler #1 is a 1,300 PSIG, 950 °F/ 609.6 mmbtu/hr rated unit which serves Turbine #1 which has a gross 55 

MW capacity. The boiler and turbine was installed in 1960. Boiler #2 is the same as Boiler #1, except it was 

designed for a steam heat input of 627.3 mmbtu/hr and was installed in 1962. It serves Turbine #2 which has a gross 

capacity rating of 51 MW. Boiler #3 is a supercritical, 3,653 psig/1005 oF boiler with a design heat input of 4,094.1 

mmbtu/hour. The boiler serves Turbine #3 which has a gross capacity of 400.6 MW. This boiler and turbine was 

installed in 1969. The boilers burn a blend of coal typically 85% Powder River Basin (PRB) (sub bituminous) and 

15% bituminous coal. Sibley #3 also burns tire derived fuel however normally this is less than 1% of the fuel being 

burned. Boilers #1 and 2 have burned biofuel in the past as a test burn but are not currently permitted for burning 

biofuel.

Sibley Units 1 & 2 utilizes electrostatic precipitators (ESP), over fire air (OFA) and selective non-catalytic 

reduction/rich reagent injection (SNCR/RRI) as pollution control devices. Sibley #3 has an ESP, OFA and SCR for 

pollution control devices.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: FRS #:

SCC / Description 10100203 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Cyclone Furnace (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 162 0 0 0 3600 3600 4 12

Wednesday, February 16, 2011 Page 2 of 13
KCP&L GMO Sibley Units 1, 2, and 3 ICR Testing

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.

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Inorganic (Aqueous) 

Condensible Part.

Stack OTM - 27/28 3 240 0

Organic Condensible 

Particulate

Stack OTM - 27/28 3 240 0

Stack Filterable PM2.5 OTM - 27/28 3 240 0

Stack Total Particulate OTM - 27/28 0

Stack Lead Method 29 3 240 0

Stack Chromium Method 29 3 240 0

Stack Manganese Method 29 3 240 0

Stack Cobalt Method 29 3 240 0

Stack Nickel Method 29 3 240 0

Stack Arsenic Method 29 3 240 0

Stack Selenium Method 29 3 240 0

Stack Beryllium Method 29 3 240 0

Stack Antimony Method 29 3 240 0

Stack Filterable Particulate Method 29 3 240 0 Filterable PM

Stack Cadmium Method 29 3 240 0

Stack O2 Method 3A O2 3 240 0

Stack Co2 Method 3A CO2 3 240 0

Mercury Method 30B 3 120 0 See OETM 

spreadsheet for results

Stack

Wednesday, February 16, 2011 Page 3 of 13
KCP&L GMO Sibley Units 1, 2, and 3 ICR Testing

Sampling / Stack Data Results Summary

Location Stack - Method 29

Average

Run Number 1 2 3

Test Date 3/16/2010 3/16/2010 3/17/2010

Run Start Time 2:30:00 PM 9:03:00 PM 12:05:00 PM

Run Finish Time 2:30:00 PM 3/17/2010 

1:49:00 

AM

4:48:00 PM

Net Run Time, minutes 164.52 240 240

Dry Gas Meter Volume Sampled, dscf 185.974 262.911 275.625 241.503

Moisture Content of Stack Gas, % 12.17 12.74 12.36 12.423

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

Carbon Dioxide, % 16.1 16 16 16.033

Oxygen, % 3.4 3.3 3.3 3.333

Average Stack Gas Temperature, °F 287.44 290.58 291.17 289.730

Dry Volumetric Flow Rate, dry scfm 923,629.8 871,026.2 882,832.8 892,496.267

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,542,809.4 1,472,127.4 1,493,512.3 1,502,816.36

7

Percent Isokinetic of Sampling Rate, % 92.8 95.4 98.7 95.633

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

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack - Method 3A CO2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Wednesday, February 16, 2011 Page 4 of 13
KCP&L GMO Sibley Units 1, 2, and 3 ICR Testing

Location Stack - 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 - OTM - 27/28

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Wednesday, February 16, 2011 Page 5 of 13
KCP&L GMO Sibley Units 1, 2, and 3 ICR Testing

Emissions Summary

Location: Stack - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.00148 0.00281 0.0027 0.002

lb/mmBtuO2 2.05E-07 2.74E-07 2.51E-07 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.01157 0.02 0.01946 0.017

lb/mmBtuO2 1.60E-06 1.95E-06 1.81E-06 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.00033 0.00054 0.00055 0.000

lb/mmBtuO2 4.57E-08 5.26E-08 5.11E-08 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.00049 0.00115 0.00093 0.001

lb/mmBtuO2 6.78E-08 1.12E-07 8.64E-08 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.01429 0.02303 0.02085 0.019

lb/mmBtuO2 1.98E-06 2.24E-06 1.94E-06 0.000

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.00356 0.00738 0.00784 0.006

lb/mmBtuO2 4.93E-07 7.19E-07 7.28E-07 0.000

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 65.8 95.5 98.9 86.733

lb/mmBtuO2 9.11E-03 9.30E-03 9.19E-03 0.009

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.01262 0.0234 0.02536 0.020

lb/mmBtuO2 1.75E-06 2.28E-06 2.36E-06 0.000

Compound: Manganese

Average

Wednesday, February 16, 2011 Page 6 of 13
KCP&L GMO Sibley Units 1, 2, and 3 ICR Testing

Process Run Data

RunNumber 1 2 3

Mass_mg 0.01585 0.02374 0.02474 0.021

lb/mmBtuO2 2.19E-06 2.31E-06 2.30E-06 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.01586 0.02872 0.02283 0.022

lb/mmBtuO2 2.20E-06 2.80E-06 2.12E-06 0.000

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.03397 0.07063 0.07904 0.061

lb/mmBtuO2 4.70E-06 6.88E-06 7.34E-06 0.000

Location: Stack - OTM - 27/28

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 11.8 15.1 13.3 13.400

lb/mmBtuO2 3.35E-03 4.29E-03 3.71E-03 0.004

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 55.8 66.4 70.6 64.267

lb/mmBtuO2 1.59E-02 1.89E-02 1.97E-02 0.018

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 3.5 4.9 5.7 4.700

lb/mmBtuO2 9.94E-04 1.39E-03 1.59E-03 0.001

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 80.8 96.4 98.9 92.033

lb/mmBtuO2 2.30E-02 2.74E-02 2.76E-02 0.026

Wednesday, February 16, 2011 Page 7 of 13
KCP&L GMO Sibley Units 1, 2, and 3 ICR Testing

Process Run Data

APCD Run Data

Run Name Value UOM Comments

Target

Value

1 Unit 1 Load 45 MW 0 start of run

1 Unit 2 Load 45 MW 0 start of run

1 Unit 3 Load 350 MW 0 start of run

2 Unit 1 Load 45 MW 0 start of run

2 Unit 2 Load 45 MW 0 start of run

2 Unit 3 Load 352 MW 0 start of run

3 Unit 1 Load 45 MW 0 start of run

3 Unit 2 Load 45 MW 0 start of run

3 Unit 3 Load 350 MW 0 start of run

1 Bituminous Coal Burned 0 Tons 0

Run Name Value UOM Comments

Target

Value

1 Unit 1 ELECTROSTATIC PRECIPITATOR 411.4Avg Primary Voltage 0

2 Unit 1 ELECTROSTATIC PRECIPITATOR 397Avg Primary Voltage 0

3 Unit 1 ELECTROSTATIC PRECIPITATOR 409.4Avg Primary Voltage 0

1 OVERFIRE AIR 0 0

2 OVERFIRE AIR 0 0

3 OVERFIRE AIR 0 0

1 Unit 2 SELECTIVE NONCATALYTIC 

REDUCTION FOR NOX w/ Rich Reagent 

Reinjection

60.5 GPH 0

2 Unit 2 SELECTIVE NONCATALYTIC 

REDUCTION FOR NOX w/ Rich Reagent 

Reinjection

60.5 GPH 0

3 Unit 2 SELECTIVE NONCATALYTIC 

REDUCTION FOR NOX w/ Rich Reagent 

Reinjection

60.2 GPH 0

1 Unit 3 SCR (SELECTIVE CATALYTIC 

REDUCTION)

249.85 GPH 0

2 Unit 3 SCR (SELECTIVE CATALYTIC 

REDUCTION)

250.65 GPH 0

3 Unit 3 SCR (SELECTIVE CATALYTIC 

REDUCTION)

259.3 GPH 0

1 Unit 2 ELECTROSTATIC PRECIPITATOR 401.2Avg Primary Voltage 0

2 Unit 2 ELECTROSTATIC PRECIPITATOR 397.6Avg Primary Voltage 0

3 Unit 2 ELECTROSTATIC PRECIPITATOR 389.4Avg Primary Voltage 0

Wednesday, February 16, 2011 Page 8 of 13
KCP&L GMO Sibley Units 1, 2, and 3 ICR Testing

Process Lab Run Data

1 Unit 3 ELECTROSTATIC PRECIPITATOR 470.38Avg Primary Voltage 0

2 Unit 3 ELECTROSTATIC PRECIPITATOR 469.94Avg Primary Voltage 0

3 Unit 3 ELECTROSTATIC PRECIPITATOR 473.13Avg Primary Voltage 0

1 Unit 1 SELECTIVE NONCATALYTIC 

REDUCTION FOR NOX w/ Rich Reagent 

Reinjection

61.7 GPH 0

2 Unit 1 SELECTIVE NONCATALYTIC 

REDUCTION FOR NOX w/ Rich Reagent 

Reinjection

60.5 GPH 0

3 Unit 1 SELECTIVE NONCATALYTIC 

REDUCTION FOR NOX w/ Rich Reagent 

Reinjection

60.2 GPH 0

2 0 0

3 0 0

Wednesday, February 16, 2011 Page 9 of 13
KCP&L GMO Sibley Units 1, 2, and 3 ICR Testing

Sampling / Stack Data Results Detail

Location Stack - Method 29

Average

Run Number 1 2 3

Test Date 3/16/2010 3/16/2010 3/17/2010

Run Start Time 2:30:00 PM 9:03:00 PM 12:05:00 PM

Run Finish Time 2:30:00 PM 3/17/2010 

1:49:00 AM

4:48:00 PM

Net Traversing Points 9 12 12

Net Run Time, minutes 164.52 240 240

Nozzle Diameter, inches 0.186 0.186 0.186 0.186

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9734 0.9779 0.9779 0.976

Barometric Pressure, inches of Mercury 29.16 29.13 29.15 29.147

Average Orifice Meter Differential, inches H2O 4.76 4.42 4.87 4.683

Dry Gas Meter Volume Sampled, cubic feet 196.525 276.805 290.795 254.708

Average Dry Gas Meter Temperature, °F 75.67 75.17 77.25 76.030

Dry Gas Meter Volume Sampled, dscf 185.974 262.911 275.625 241.503

Total Moisture Liquid collected, g 547.4 815.1 825.8 729.433

Volume of Water Vapor, standard cubic feet 25.77 38.37 38.87 34.337

Moisture Content of Stack Gas, % 12.17 12.74 12.36 12.423

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

Dry Mole Fraction 0.8783 0.8726 0.8764 0.876

Carbon Dioxide, % 16.1 16 16 16.033

Oxygen, % 3.4 3.3 3.3 3.333

Carbon Monoxide & Nitrogen, % 80.5 80.7 80.7 80.633

Fuel Factor 1.09 1.10 1.10

Dry Molecular Weight, lb/lb-Mole 30.71 30.69 30.69 30.697

Wet Molecular weight, lb/lb-Mole 29.16 29.07 29.12 29.117

Flue Gas Static Pressure, inches of H2O -4 -4 -6 -4.667

Absolute Flue Gas Pressure, inches of Mercury 28.87 28.84 28.71 28.807

Average Stack Gas Temperature, °F 287.44 290.58 291.17 289.730

Average Velocity Head, inches of H2O 7.0484919817

9341

6.363917615

86831

6.526376007

51546

6.646

Average Stack Gas Velocity, feet/second 179.64 171.41 173.90 174.983

Stack Cross-Sectional Area, square feet 143.139 143.139 143.139 143.139

Dry Volumetric Flow Rate, dry scfm 923,629.8 871,026.2 882,832.8 892,496.267

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,542,809.4 1,472,127.4 1,493,512.3 1,502,816.3

67

Percent Isokinetic of Sampling Rate, % 92.8 95.4 98.7 95.633

Percent Excess Air, % 19.0 18.3 18.3 18.533

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

Round Duct Diameter, inches 162 162 162

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Wednesday, February 16, 2011 Page 10 of 13
KCP&L GMO Sibley Units 1, 2, and 3 ICR Testing

Location Stack - Method 3A CO2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Wednesday, February 16, 2011 Page 11 of 13
KCP&L GMO Sibley Units 1, 2, and 3 ICR Testing

Location Stack - Method 3A O2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Wednesday, February 16, 2011 Page 12 of 13
KCP&L GMO Sibley Units 1, 2, and 3 ICR Testing

Location Stack - OTM - 27/28

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Wednesday, February 16, 2011 Page 13 of 13