Name: Ms. Tiffany Le

Title: Senior Environmental Scientist

Company: Kansas City Board of Public Utilities

Sign Date:

Name: Mr. Jeremy Miller

Title: Lead Field Engineer

Company: GE International, Inc.

Sign Date:

Permitted Facility Representative / Date Testing Company Representative / Date

Kansas City Board of Public 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.

Wednesday, February 23, 2011 Page 1 of 11
Kansas City Board of Public Utilities

Facility Information:

Quindaro Power Station

3601 North 12th Street

Kansas City KS 66104

Contact: Ms. Tiffany Le

Phone: 913-573-9789

Fax: 913-328-6281

Email: tle@bpu.com

Testing Company:

GE International, Inc.

888 Industrial Drive

Elmhurst IL 60126

Contact:Mr. Jeremy Miller

Phone: 219-838-6082

Fax: 219-838-6083

Email: jeremy1.miller@ge.com

Air Permit Number:

2090048

Permitted Source ID/Name:

1295 Quindaro Power Station

Permitted Maximum Process Rate:

144 MW

Max. Normal Operation Process Rate:

119 MW

Target Process Test Rate

100 MW

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

 process flow diagram:

The flue gas is controlled via an Electrostatic Precipitator.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 2020900048 FRS #: 110000445368

SCC / Description

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

Unit 2 Stack 159.96 0 0 0 624 2940 4 24

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Unit 2 Stack Cadmium Method 29 3 240 0

Unit 2 Stack Lead Method 29 3 240 0

Unit 2 Stack Nickel Method 29 3 240 0

Unit 2 Stack Antimony Method 29 3 240 0

Unit 2 Stack Manganese Method 29 3 240 0

Unit 2 Stack Chromium Method 29 3 240 0

Unit 2 Stack Beryllium Method 29 3 240 0

Unit 2 Stack Arsenic Method 29 3 240 0

Wednesday, February 23, 2011 Page 2 of 11
Kansas City Board of Public Utilities

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.

Because of the port parameters OTM27/OTM28 was supplanted with M5/OTM28. Teflon liners were also used as a 

precaution due to the long port lengths and subsequently long particulate probes. Both modifications had prior EPA 

approval.

Unit 2 Stack Selenium Method 29 3 240 0

Unit 2 Stack Cobalt Method 29 3 240 0

Unit 2 Stack Co2 Method 3A CO2 3 400 0

Unit 2 Stack O2 Method 3A O2 3 400 0

Unit 2 Stack Filterable Particulate Method 5/OTM-28 3 240 0

Unit 2 Stack Total Particulate Method 5/OTM-28 3 240 0

Organic Condensible 

Particulate

Unit 2 Stack Method 5/OTM-28 3 240 0

Inorganic (Aqueous) 

Condensible Part.

Unit 2 Stack Method 5/OTM-28 3 240 0

Unit 2 Stack Filterable Particulate Method 5 3 240 0

Wednesday, February 23, 2011 Page 3 of 11
Kansas City Board of Public Utilities

Sampling / Stack Data Results Summary

Location Unit 2 Stack - Method 29

Average

Run Number 1 2 3

Test Date 6/15/2010 6/16/2010 6/18/2010

Run Start Time 2:40:00 PM 8:50:00 

AM

9:35:00 AM

Run Finish Time 8:10:00 PM 2:00:00 PM 2:40:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 142.909 142.898 136.690 140.832

Moisture Content of Stack Gas, % 10.70 11.10 10.54 10.780

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

Carbon Dioxide, % 11.8 12.4 11.3 11.833

Oxygen, % 8.2 7.7 8.8 8.233

Average Stack Gas Temperature, °F 310.90 313.44 303.85 309.397

Dry Volumetric Flow Rate, dry scfm 268,394.3 266,684.3 258,136.9 264,405.167

Actual Wet Volumetric Flue Gas Flow Rate, acfm 456,518.9 455,095.4 434,580.5 448,731.600

Percent Isokinetic of Sampling Rate, % 101.1 101.7 100.5 101.100

F-Factor, dscfm/MMBtu @ %O2 10025 9031 9275 9,443.667

Fw 0 0 0 0.000

Fc 1901 1797 1833 1,843.667

Wednesday, February 23, 2011 Page 4 of 11
Kansas City Board of Public Utilities

Location Unit 2 Stack - Method 5

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 Unit 2 Stack - Method 5/OTM-28

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Wednesday, February 23, 2011 Page 5 of 11
Kansas City Board of Public Utilities

Emissions Summary

Location: Unit 2 Stack - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.0028 0.0028 0.00298 0.003

lb/mmBtuO2 7.13E-07 6.18E-07 7.70E-07 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.00679 0.00747 0.00903 0.008

lb/mmBtuO2 1.73E-06 1.65E-06 2.33E-06 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.00097 0.00099 0.00131 0.001

lb/mmBtuO2 2.47E-07 2.18E-07 3.38E-07 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.00092 0.00132 0.00125 0.001

lb/mmBtuO2 2.34E-07 2.91E-07 3.23E-07 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.00983 0.00984 0.02837 0.016

lb/mmBtuO2 2.50E-06 2.17E-06 7.33E-06 0.000

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.00405 0.00431 0.00725 0.005

lb/mmBtuO2 1.03E-06 9.51E-07 1.87E-06 0.000

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.01479 0.01349 0.01949 0.016

lb/mmBtuO2 3.76E-06 2.98E-06 5.04E-06 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.03923 0.04533 0.05883 0.048

lb/mmBtuO2 9.98E-06 1.00E-05 1.52E-05 0.000

Compound: Nickel

Average

Wednesday, February 23, 2011 Page 6 of 11
Kansas City Board of Public Utilities

Process Run Data

RunNumber 1 2 3

Mass_mg 0.01337 0.01207 0.04187 0.022

lb/mmBtuO2 3.40E-06 2.66E-06 1.08E-05 0.000

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.0164 0.0232 0.0147 0.018

lb/mmBtuO2 4.17E-06 5.12E-06 3.80E-06 0.000

Location: Unit 2 Stack - Method 5

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 79.7 81 159.8 106.833

lb/mmBtuO2 2.03E-02 1.79E-02 4.13E-02 0.027

Location: Unit 2 Stack - Method 5/OTM-28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 90.6 99.2 177.7 122.500

lb/mmBtuO2 2.34E-02 2.19E-02 4.53E-02 0.030

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 18.02 20.32 13.82 17.387

lb/mmBtuO2 4.66E-03 4.49E-03 3.52E-03 0.004

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 4.08 4.08 3.38 3.847

lb/mmBtuO2 1.05E-03 9.01E-04 8.61E-04 0.001

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 112.7 123.6 194.9 143.733

lb/mmBtuO2 2.91E-02 2.73E-02 4.97E-02 0.035

Wednesday, February 23, 2011 Page 7 of 11
Kansas City Board of Public Utilities

Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Coal Firing Rate 0.0545 1000 tons/hr 0

1 Gross Megawatt 92.9 MW/hr 0

1 Heat Input 1152 MMBtu/hr 0

2 Coal Firing Rate 0.0562 1000 tons/hr 0

2 Gross Megawatt 96.1 MW/hr 0

2 Heat Input 1157.1 MMBtu/hr 0

3 Coal Firing Rate 0.05 1000 tons/hr 0

3 Gross Megawatt 85.1 MW/hr 0

3 Heat Input 1084.5 MMBtu/hr 0

Run Name Value UOM Comments

Target

Value

1 LOW NOX BURNERS 0 0

1 ELECTROSTATIC PRECIPITATOR 0 0

Wednesday, February 23, 2011 Page 8 of 11
Kansas City Board of Public Utilities

Sampling / Stack Data Results Detail

Location Unit 2 Stack - Method 29

Average

Run Number 1 2 3

Test Date 6/15/2010 6/16/2010 6/18/2010

Run Start Time 2:40:00 PM 8:50:00 AM 9:35:00 AM

Run Finish Time 8:10:00 PM 2:00:00 PM 2:40:00 PM

Net Traversing Points 48 48 48

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.237 0.237 0.237 0.237

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.009 1.009 1.009 1.009

Barometric Pressure, inches of Mercury 28.82 28.95 28.8 28.857

Average Orifice Meter Differential, inches H2O 1.13 1.13 1.04 1.100

Dry Gas Meter Volume Sampled, cubic feet 152.901 153.391 147.480 151.257

Average Dry Gas Meter Temperature, °F 90.63 94.92 94.76 93.437

Dry Gas Meter Volume Sampled, dscf 142.909 142.898 136.690 140.832

Total Moisture Liquid collected, g 363.9 379.1 342.2 361.733

Volume of Water Vapor, standard cubic feet 17.13 17.84 16.11 17.027

Moisture Content of Stack Gas, % 10.70 11.10 10.54 10.780

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

Dry Mole Fraction 0.893 0.889 0.8946 0.892

Carbon Dioxide, % 11.8 12.4 11.3 11.833

Oxygen, % 8.2 7.7 8.8 8.233

Carbon Monoxide & Nitrogen, % 80 79.9 79.9 79.933

Fuel Factor 1.08 1.06 1.07

Dry Molecular Weight, lb/lb-Mole 30.22 30.29 30.16 30.223

Wet Molecular weight, lb/lb-Mole 28.91 28.93 28.88 28.907

Flue Gas Static Pressure, inches of H2O -0.8 -0.8 -0.8 -0.800

Absolute Flue Gas Pressure, inches of Mercury 28.76 28.89 28.74 28.797

Average Stack Gas Temperature, °F 310.90 313.44 303.85 309.397

Average Velocity Head, inches of H2O 0.6215814451

12051

0.619001810

022396

0.567514184

986363

0.603

Average Stack Gas Velocity, feet/second 54.52 54.35 51.90 53.590

Stack Cross-Sectional Area, square feet 139.557 139.557 139.557 139.557

Dry Volumetric Flow Rate, dry scfm 268,394.3 266,684.3 258,136.9 264,405.167

Actual Wet Volumetric Flue Gas Flow Rate, acfm 456,518.9 455,095.4 434,580.5 448,731.600

Percent Isokinetic of Sampling Rate, % 101.1 101.7 100.5 101.100

Percent Excess Air, % 63.5 57.5 71.6 64.200

F-Factor, dscfm/MMBtu @ %O2 10025 9031 9275 9,443.667

Round Duct Diameter, inches 159.96 159.96 159.96

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 0 0 0 0.000

Fc 1901 1797 1833 1,843.667

Wednesday, February 23, 2011 Page 9 of 11
Kansas City Board of Public Utilities

Location Unit 2 Stack - Method 5

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 23, 2011 Page 10 of 11
Kansas City Board of Public Utilities

Location Unit 2 Stack - Method 5/OTM-28

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Wednesday, February 23, 2011 Page 11 of 11