Name:

Title:

Company:

Sign Date:

Name:

Title:

Company:

Sign Date:

Permitted Facility Representative / Date Testing Company Representative / Date

KCP&L Hawthorn Unit 5A

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 34
KCP&L Hawthorn Unit 5A

Facility Information:

2079_Hawthorn_5A

8700 Hawthorne Rd

Kansas City MO 64120

Contact: Michael McMenus

Phone: (816) 242-3549

Fax:

Email: Michael.McMenus@kcpl.com

Testing Company:

Civil & Environmental Consultants, Inc.

4848 Park 370 Blvd

Hazelwood MO 63042

Contact: Frank Stevens

Phone: (314) 656-4566

Fax: (314) 656-4595

Email: fstevens@cecinc.com

Air Permit Number:

2079

Permitted Source ID/Name:

095-0022 Kansas City Power& Light Co (Hawthorn)

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:

KCPL Hawthorn Power Station is located on a 550-acre site northeast of downtown Kansas City, Missouri. 

Hawthorn Unit 5A is designed for firing either pulverized coal or natural gas and is a natural circulation, balanced 

draft, sub-critical boiler. Unit 5A is a 594 megawatt boiler that is primarily fired with Powder River Basin (PRB) 

coal. It is equipped with Babcock & Wilcox Company (B&W) DRBZ 2 Low Nox Burners with over fire air. The 

burners are configured in an opposing wall fired array. The unit uses Selective Catalytic Reduction (SCR) for Nox 

control, a spray dry flue gas desulfurization (FGD) system for SO2 control and a pulse-jet baghouse for particulate 

control. Stack discharge temperature is approximately 180 degrees F.

Industry/SCC/NAIS

Sampling Location Information:

Test Parameter Information:

AFS #: FRS #:

SCC / Description 10100226 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Pulverized Coal: Dry Bottom Tangential (Subbituminous 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 243.6 0 0 0 4800 1680 4 16

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack % H2O Method 1 - 4 3 120 0

Stack Flowrate Method 1 - 4 3 120 0

Stack Carbon Monoxide Method 10 3 120 0

Wednesday, February 16, 2011 Page 2 of 34
KCP&L Hawthorn Unit 5A

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.

None.

Total organic compounds 

(TOC) as Propane

Stack Method 25A 3 120 0

Stack Hydrogen Chloride Method 26A 3 180 0

Stack Hydrogen Fluoride Method 26A 3 180 0

Stack Filterable Particulate OTM - 27/28 3 240 0

Stack Total Particulate OTM - 27/28 3 240 0

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 PM2.5 OTM - 27/28 3 240 0

Stack Antimony Method 29 3 240 0

Stack Selenium Method 29 3 240 0

Stack Nickel Method 29 3 240 0

Stack Lead Method 29 3 240 0

Stack Filterable Particulate Method 29 3 240 0

Stack Arsenic Method 29 3 240 0

Stack Cobalt Method 29 3 240 0

Stack Chromium Method 29 3 240 0

Stack Beryllium Method 29 3 240 0

Stack Cadmium Method 29 3 240 0

Stack Manganese Method 29 3 240 0

Co2 Method 3A CO2 9 120 0 R1-R3, 120min; R4-

R6, 180min; R7-R9, 

240min

Stack

O2 Method 3A O2 9 120 0 R1-R3, 120min; R4-

R6, 180min; R7-R9, 

240min

Stack

Stack Sulfur Dioxide Method 6C 3 180 0

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

Wednesday, February 16, 2011 Page 3 of 34
KCP&L Hawthorn Unit 5A

Sampling / Stack Data Results Summary

Location Stack - 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

Location Stack - 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

Wednesday, February 16, 2011 Page 4 of 34
KCP&L Hawthorn Unit 5A

Location Stack - Method 26A

Average

Run Number 1 2 3

Test Date 4/22/2010 4/23/2010 4/24/2010

Run Start Time 7:34:00 PM 8:52:00 

AM

7:35:00 PM

Run Finish Time 10:57:00 PM 4/24/2010 

6:59:00 PM

11:07:00 PM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 132.281 132.814 120.994 128.696

Moisture Content of Stack Gas, % 15.03 15.12 15.52 15.223

Moisture Saturation at Stack Gas Temperature, % 61.10 61.72 59.96 60.927

Carbon Dioxide, % 13.8 13.5 12.5 13.267

Oxygen, % 5.7 5.7 6.9 6.100

Average Stack Gas Temperature, °F 186.19 186.69 184.75 185.877

Dry Volumetric Flow Rate, dry scfm 1,239,766.4 1,228,698.9 1,221,987.9 1,230,151.06

7

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,866,777.3 1,852,212.8 1,870,078.6 1,863,022.90

0

Percent Isokinetic of Sampling Rate, % 100.6 101.9 93.3 98.600

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

Wednesday, February 16, 2011 Page 5 of 34
KCP&L Hawthorn Unit 5A

Location Stack - 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 - 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 6 of 34
KCP&L Hawthorn Unit 5A

Location Stack - 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 - 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

Wednesday, February 16, 2011 Page 7 of 34
KCP&L Hawthorn Unit 5A

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 - 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

Wednesday, February 16, 2011 Page 8 of 34
KCP&L Hawthorn Unit 5A

Location Stack - 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 - 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

Wednesday, February 16, 2011 Page 9 of 34
KCP&L Hawthorn Unit 5A

Location Stack - 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

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 10 of 34
KCP&L Hawthorn Unit 5A

Emissions Summary

Location: Stack - Method 10 

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 1.49E-01 7.26E-02 7.63E-02 0.099

ppm 1.53E+02 7.42E+01 7.80E+01 101.733

ppm@7%O2 1.39E+02 6.79E+01 7.13E+01 92.733

Location: Stack - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 1.72E-04 5.79E-04 3.96E-04 0.000

ppm 1.12E-01 3.76E-01 2.57E-01 0.248

ppm@7%O2 1.02E-01 3.44E-01 2.35E-01 0.227

Location: Stack - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 0.304 0.329 0.281 0.305

lb/mmBtuO2 6.81E-05 7.34E-05 7.48E-05 0.000

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.311 0.337 0.288 0.312

lb/mmBtuO2 6.97E-05 7.52E-05 7.66E-05 0.000

Location: Stack - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.00746 0.00109 0.00052 0.003

lb/mmBtuO2 1.21E-06 1.87E-07 8.90E-08 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.00187 0.0022 0.00133 0.002

lb/mmBtuO2 3.05E-07 3.77E-07 2.28E-07 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.00044 0.00044 0.00044 0.000

lb/mmBtuO2 7.17E-08 7.54E-08 7.53E-08 0.000

Wednesday, February 16, 2011 Page 11 of 34
KCP&L Hawthorn Unit 5A

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.00115 0.00475 0.00043 0.002

lb/mmBtuO2 1.87E-07 8.14E-07 7.36E-08 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.00764 0.0071 0.0073 0.007

lb/mmBtuO2 1.24E-06 1.22E-06 1.25E-06 0.000

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.00405 0.00426 0.00219 0.004

lb/mmBtuO2 6.60E-07 7.30E-07 3.75E-07 0.000

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 4.7 5.1 7.4 5.733

lb/mmBtuO2 7.65E-04 8.73E-04 1.27E-03 0.001

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.0233 0.01021 0.00581 0.013

lb/mmBtuO2 3.79E-06 1.75E-06 9.94E-07 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.01105 0.00642 0.00529 0.008

lb/mmBtuO2 1.80E-06 1.10E-06 9.05E-07 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.00516 0.00576 0.0072 0.006

lb/mmBtuO2 8.40E-07 9.86E-07 1.23E-06 0.000

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.00276 0.00277 0.00277 0.003

lb/mmBtuO2 4.49E-07 4.74E-07 4.74E-07 0.000

Location: Stack - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

lb/mmBtuCO2 9.43E-02 1.15E-01 1.61E-01 0.123

Wednesday, February 16, 2011 Page 12 of 34
KCP&L Hawthorn Unit 5A

Process Run Data

ppm 4.35E+01 5.19E+01 6.71E+01 54.167

ppm@7%O2 3.98E+01 4.75E+01 6.66E+01 51.300

Location: Stack - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

lb/mmBtuO2 8.03E-02 6.41E-02 7.87E-02 0.074

ppm 5.00E+01 3.99E+01 4.51E+01 45.000

ppm@7%O2 4.57E+01 3.65E+01 4.48E+01 42.333

Location: Stack - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 3 4.1 3.4 3.500

lb/mmBtuO2 1.06E-03 1.43E-03 1.22E-03 0.001

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 2.2 1.4 2.6 2.067

lb/mmBtuO2 7.74E-04 4.89E-04 9.34E-04 0.001

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 19.2 17.1 11 15.767

lb/mmBtuO2 6.76E-03 5.98E-03 3.95E-03 0.006

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 6.1 4.8 7.4 6.100

lb/mmBtuO2 2.15E-03 1.68E-03 2.66E-03 0.002

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 28.3 26 22 25.433

lb/mmBtuO2 9.96E-03 9.09E-03 7.90E-03 0.009

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 27.5 23.3 21 23.933

lb/mmBtuO2 9.68E-03 8.14E-03 7.54E-03 0.008

Wednesday, February 16, 2011 Page 13 of 34
KCP&L Hawthorn Unit 5A

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Subbituminous Coal Burned 5441 Tons Organic HAP Run 

1

0

1 Steam Output 3267.4 1000 lb steam/hr Organic HAP Run 

1

0

1 Unit Net Electric Generation 525.1 MWh Organic HAP Run 

1

0

1 Unit Gross Electrical Output 549 MW Organic HAP Run 

1

0

2 Subbituminous Coal Burned 5455.2 Tons Organic HAP Run 

2

0

2 Steam Output 3323.6 1000 lb steam/hr Organic HAP Run 

2

0

2 Unit Net Electric Generation 531.9 MWh Organic HAP Run 

2

0

2 Unit Gross Electrical Output 556.4 MW Organic HAP Run 

2

0

3 Subbituminous Coal Burned 5455.2 Tons Organic HAP Run 

3

0

3 Steam Output 3323.6 1000 lb steam/hr Organic HAP Run 

3

0

3 Unit Net Electric Generation 531.9 MWh Organic HAP Run 

3

0

3 Unit Gross Electrical Output 556.4 MW Organic HAP Run 

3

0

4 Subbituminous Coal Burned 5348.1 Tons Acid Gas HAP 

Run 1

0

4 Steam Output 2991 1000 lb steam/hr Acid Gas HAP 

Run 1

0

4 Unit Net Electric Generation 475.4 MWh Acid Gas HAP 

Run 1

0

4 Unit Gross Electrical Output 498.8 MW Acid Gas HAP 

Run 1

0

5 Subbituminous Coal Burned 6314.5 Tons Acid Gas HAP 

Run 2

0

5 Steam Output 2701.3 1000 lb steam/hr Acid Gas HAP 

Run 2

0

5 Unit Net Electric Generation 424.2 MWh Acid Gas HAP 

Run 2

0

5 Unit Gross Electrical Output 446.3 MW Acid Gas HAP 

Run 2

0

6 Subbituminous Coal Burned 6314.5 Tons Acid Gas HAP 

Run 3

0

Wednesday, February 16, 2011 Page 14 of 34
KCP&L Hawthorn Unit 5A

APCD Run Data

6 Steam Output 2701.3 1000 lb steam/hr Acid Gas HAP 

Run 3

0

6 Unit Net Electric Generation 424.2 MWh Acid Gas HAP 

Run 3

0

6 Unit Gross Electrical Output 446.3 MW Acid Gas HAP 

Run 3

0

7 Subbituminous Coal Burned 5194.3 Tons Metal PM HAP 

Run 1

0

7 Steam Output 3328.8 1000 lb steam/hr Metal PM HAP 

Run 1

0

7 Unit Net Electric Generation 528.4 MWh Metal PM HAP 

Run 1

0

7 Unit Gross Electrical Output 552.7 MW Metal PM HAP 

Run 1

0

8 Subbituminous Coal Burned 5194.3 Tons Metal PM HAP 

Run 2

0

8 Steam Output 3328.8 1000 lb steam/hr Metal PM HAP 

Run 2

0

8 Unit Net Electric Generation 528.4 MWh Metal PM HAP 

Run 2

0

8 Unit Gross Electrical Output 552.7 MW Metal PM HAP 

Run 2

0

9 Subbituminous Coal Burned 5194.3 Tons Metal PM HAP 

Run 3

0

9 Steam Output 3328.8 1000 lb steam/hr Metal PM HAP 

Run 3

0

9 Unit Net Electric Generation 528.4 MWh Metal PM HAP 

Run 3

0

9 Unit Gross Electrical Output 552.7 MW Metal PM HAP 

Run 3

0

Run Name Value UOM Comments

Target

Value

1 DRY SCRUBBER 379.5 FGD scrubber flow (gpm)0

2 DRY SCRUBBER 373.7 FGD scrubber flow (gpm)0

3 DRY SCRUBBER 373.7 FGD scrubber flow (gpm)0

4 DRY SCRUBBER 360.8 FGD scrubber flow (gpm)0

5 DRY SCRUBBER 346.6 FGD scrubber flow (gpm)0

6 DRY SCRUBBER 346.6 FGD scrubber flow (gpm)0

7 DRY SCRUBBER 394.2 FGD scrubber flow (gpm)0

8 DRY SCRUBBER 394.2 FGD scrubber flow (gpm)0

9 DRY SCRUBBER 394.2 FGD scrubber flow (gpm)0

Wednesday, February 16, 2011 Page 15 of 34
KCP&L Hawthorn Unit 5A

Process Lab Run Data

1 FABRIC FILTER 0 0

2 FABRIC FILTER 0 0

3 FABRIC FILTER 0 0

4 FABRIC FILTER 0 0

5 FABRIC FILTER 0 0

6 FABRIC FILTER 0 0

7 FABRIC FILTER 0 0

8 FABRIC FILTER 0 0

9 FABRIC FILTER 0 0

1 OVERFIRE AIR 0 0

2 OVERFIRE AIR 0 0

3 OVERFIRE AIR 0 0

4 OVERFIRE AIR 0 0

5 OVERFIRE AIR 0 0

6 OVERFIRE AIR 0 0

7 OVERFIRE AIR 0 0

8 OVERFIRE AIR 0 0

9 OVERFIRE AIR 0 0

1 SCR (SELECTIVE CATALYTIC REDUCTION) 0 0

2 SCR (SELECTIVE CATALYTIC REDUCTION) 0 0

3 SCR (SELECTIVE CATALYTIC REDUCTION) 0 0

4 SCR (SELECTIVE CATALYTIC REDUCTION) 0 0

5 SCR (SELECTIVE CATALYTIC REDUCTION) 0 0

6 SCR (SELECTIVE CATALYTIC REDUCTION) 0 0

7 SCR (SELECTIVE CATALYTIC REDUCTION) 0 0

8 SCR (SELECTIVE CATALYTIC REDUCTION) 0 0

9 SCR (SELECTIVE CATALYTIC REDUCTION) 0 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value (HHV as received) 9360 Btu/lb

2 Fuel Higher Heating Value (HHV as received) 9216 Btu/lb

3 Fuel Higher Heating Value (HHV as received) 9237 Btu/lb

4 Fuel Higher Heating Value (HHV as received) 9301 Btu/lb

5 Fuel Higher Heating Value (HHV as received) 9086 Btu/lb

6 Fuel Higher Heating Value (HHV as received) 9225 Btu/lb

7 Fuel Higher Heating Value (HHV as received) 9233 Btu/lb

Wednesday, February 16, 2011 Page 16 of 34
KCP&L Hawthorn Unit 5A

8 Fuel Higher Heating Value (HHV as received) 9066 Btu/lb

9 Fuel Higher Heating Value (HHV as received) 9231 Btu/lb

1 Fuel Moisture (as received) 21.35 %

2 Fuel Moisture (as received) 22.95 %

3 Fuel Moisture (as received) 23.58 %

4 Fuel Moisture (as received) 22.27 %

5 Fuel Moisture (as received) 22.98 %

6 Fuel Moisture (as received) 22.59 %

7 Fuel Moisture (as received) 23.64 %

8 Fuel Moisture (as received) 25.48 %

9 Fuel Moisture (as received) 24.47 %

1 Fuel Mercury Content 0.073 ug/g

2 Fuel Mercury Content 0.075 ug/g

3 Fuel Mercury Content 0.079 ug/g

4 Fuel Mercury Content 0.079 ug/g

5 Fuel Mercury Content 0.086 ug/g

6 Fuel Mercury Content 0.076 ug/g

7 Fuel Mercury Content 0.076 ug/g

8 Fuel Mercury Content 0.084 ug/g

9 Fuel Mercury Content 0.09 ug/g

1 Fuel Cadmium Content 0.12 ug/g

2 Fuel Cadmium Content 0.11 ug/g

3 Fuel Cadmium Content 0.08 ug/g

4 Fuel Cadmium Content 0.11 ug/g

5 Fuel Cadmium Content 0.14 ug/g

6 Fuel Cadmium Content 0.11 ug/g

7 Fuel Cadmium Content 0.07 ug/g

8 Fuel Cadmium Content 0.07 ug/g

9 Fuel Cadmium Content 0.06 ug/g

1 Fuel Nickel Content 5 ug/g

2 Fuel Nickel Content 6 ug/g

3 Fuel Nickel Content 5 ug/g

4 Fuel Nickel Content 6 ug/g

5 Fuel Nickel Content 6 ug/g

6 Fuel Nickel Content 7 ug/g

7 Fuel Nickel Content 4 ug/g

8 Fuel Nickel Content 4 ug/g

9 Fuel Nickel Content 4 ug/g

1 Fuel Arsenic Content 1.3 ug/g

2 Fuel Arsenic Content 1.4 ug/g

3 Fuel Arsenic Content 1.2 ug/g

4 Fuel Arsenic Content 1.4 ug/g

5 Fuel Arsenic Content 1.6 ug/g

Wednesday, February 16, 2011 Page 17 of 34
KCP&L Hawthorn Unit 5A

6 Fuel Arsenic Content 1.7 ug/g

7 Fuel Arsenic Content 1.1 ug/g

8 Fuel Arsenic Content 1.2 ug/g

9 Fuel Arsenic Content 1 ug/g

1 Fuel Chromium Content 6 ug/g

2 Fuel Chromium Content 6 ug/g

3 Fuel Chromium Content 5 ug/g

4 Fuel Chromium Content 6 ug/g

5 Fuel Chromium Content 7 ug/g

6 Fuel Chromium Content 6 ug/g

7 Fuel Chromium Content 5 ug/g

8 Fuel Chromium Content 4 ug/g

9 Fuel Chromium Content 4 ug/g

1 Fuel Beryllium Content 0.2 ug/g

2 Fuel Beryllium Content 0.2 ug/g

3 Fuel Beryllium Content 0.2 ug/g

4 Fuel Beryllium Content 0.3 ug/g

5 Fuel Beryllium Content 0.3 ug/g

6 Fuel Beryllium Content 0.3 ug/g

7 Fuel Beryllium Content 0.2 ug/g

8 Fuel Beryllium Content 0.2 ug/g

9 Fuel Beryllium Content 0.2 ug/g

1 Fuel Lead Content 3.1 ug/g

2 Fuel Lead Content 2.7 ug/g

3 Fuel Lead Content 2.2 ug/g

4 Fuel Lead Content 2.4 ug/g

5 Fuel Lead Content 3 ug/g

6 Fuel Lead Content 2.7 ug/g

7 Fuel Lead Content 2.6 ug/g

8 Fuel Lead Content 2.1 ug/g

9 Fuel Lead Content 2.3 ug/g

1 Fuel Manganese Content 14 ug/g

2 Fuel Manganese Content 14 ug/g

3 Fuel Manganese Content 18 ug/g

4 Fuel Manganese Content 14 ug/g

5 Fuel Manganese Content 14 ug/g

6 Fuel Manganese Content 16 ug/g

7 Fuel Manganese Content 21 ug/g

8 Fuel Manganese Content 22 ug/g

9 Fuel Manganese Content 23 ug/g

1 Fuel Chlorine Content ug/g

2 Fuel Chlorine Content ug/g

3 Fuel Chlorine Content ug/g

Wednesday, February 16, 2011 Page 18 of 34
KCP&L Hawthorn Unit 5A

4 Fuel Chlorine Content 14 ug/g

5 Fuel Chlorine Content 10 ug/g

6 Fuel Chlorine Content 7 ug/g

7 Fuel Chlorine Content ug/g

8 Fuel Chlorine Content ug/g

9 Fuel Chlorine Content ug/g

1 Fuel Fluorine Content ug/g

2 Fuel Fluorine Content ug/g

3 Fuel Fluorine Content ug/g

4 Fuel Fluorine Content 73 ug/g

5 Fuel Fluorine Content 77 ug/g

6 Fuel Fluorine Content 69 ug/g

7 Fuel Fluorine Content ug/g

8 Fuel Fluorine Content ug/g

9 Fuel Fluorine Content ug/g

1 Fuel Antimony Content 0.16 ug/g

2 Fuel Antimony Content 0.18 ug/g

3 Fuel Antimony Content 0.14 ug/g

4 Fuel Antimony Content 0.17 ug/g

5 Fuel Antimony Content 0.2 ug/g

6 Fuel Antimony Content 0.2 ug/g

7 Fuel Antimony Content 0.14 ug/g

8 Fuel Antimony Content 0.14 ug/g

9 Fuel Antimony Content 0.15 ug/g

1 Fuel Selenium Content 0.9 ug/g

2 Fuel Selenium Content 1 ug/g

3 Fuel Selenium Content 0.9 ug/g

4 Fuel Selenium Content 0.9 ug/g

5 Fuel Selenium Content 1 ug/g

6 Fuel Selenium Content 1 ug/g

7 Fuel Selenium Content 0.9 ug/g

8 Fuel Selenium Content 1 ug/g

9 Fuel Selenium Content 0.9 ug/g

1 Fuel Cobalt Content 2.3 ppm

2 Fuel Cobalt Content 2.2 ppm

3 Fuel Cobalt Content 1.8 ppm

4 Fuel Cobalt Content 1.9 ppm

5 Fuel Cobalt Content 2.2 ppm

6 Fuel Cobalt Content 2.3 ppm

7 Fuel Cobalt Content 1.7 ppm

8 Fuel Cobalt Content 1.9 ppm

9 Fuel Cobalt Content 1.7 ppm

1 Proximate Volatiles 42.8 % by wt

Wednesday, February 16, 2011 Page 19 of 34
KCP&L Hawthorn Unit 5A

2 Proximate Volatiles 42.8 % by wt

3 Proximate Volatiles 44.41 % by wt

4 Proximate Volatiles 43.41 % by wt

5 Proximate Volatiles 43.44 % by wt

6 Proximate Volatiles 43.66 % by wt

7 Proximate Volatiles 44.57 % by wt

8 Proximate Volatiles 44.07 % by wt

9 Proximate Volatiles 44.53 % by wt

1 Proximate Ash 8.05 % by wt

2 Proximate Ash 7.99 % by wt

3 Proximate Ash 7.13 % by wt

4 Proximate Ash 8 % by wt

5 Proximate Ash 8.79 % by wt

6 Proximate Ash 8.13 % by wt

7 Proximate Ash 6.93 % by wt

8 Proximate Ash 6.67 % by wt

9 Proximate Ash 6.62 % by wt

1 Proximate Fixed Carbon 49.15 % by wt

2 Proximate Fixed Carbon 49.15 % by wt

3 Proximate Fixed Carbon 48.46 % by wt

4 Proximate Fixed Carbon 48.59 % by wt

5 Proximate Fixed Carbon 47.77 % by wt

6 Proximate Fixed Carbon 48.21 % by wt

7 Proximate Fixed Carbon 48.5 % by wt

8 Proximate Fixed Carbon 49.26 % by wt

9 Proximate Fixed Carbon 48.85 % by wt

1 Ultimate Carbon 68.54 % by wt

2 Ultimate Carbon 68.54 % by wt

3 Ultimate Carbon 69.13 % by wt

4 Ultimate Carbon 68.42 % by wt

5 Ultimate Carbon 67.9 % by wt

6 Ultimate Carbon 68.45 % by wt

7 Ultimate Carbon 69.43 % by wt

8 Ultimate Carbon 69.55 % by wt

9 Ultimate Carbon 69.81 % by wt

1 Ultimate Nitrogen 0.88 % by wt

2 Ultimate Nitrogen 0.88 % by wt

3 Ultimate Nitrogen 0.91 % by wt

4 Ultimate Nitrogen 0.88 % by wt

5 Ultimate Nitrogen 0.86 % by wt

6 Ultimate Nitrogen 0.86 % by wt

7 Ultimate Nitrogen 0.91 % by wt

8 Ultimate Nitrogen 0.93 % by wt

Wednesday, February 16, 2011 Page 20 of 34
KCP&L Hawthorn Unit 5A

9 Ultimate Nitrogen 0.93 % by wt

1 Ultimate Total Sulfur 0.33 % by wt

2 Ultimate Total Sulfur 0.33 % by wt

3 Ultimate Total Sulfur 0.41 % by wt

4 Ultimate Total Sulfur 0.44 % by wt

5 Ultimate Total Sulfur 0.48 % by wt

6 Ultimate Total Sulfur 0.49 % by wt

7 Ultimate Total Sulfur 0.42 % by wt

8 Ultimate Total Sulfur 0.4 % by wt

9 Ultimate Total Sulfur 0.38 % by wt

1 Ultimate Oxygen 17.63 % by wt

2 Ultimate Oxygen 17.63 % by wt

3 Ultimate Oxygen 17.69 % by wt

4 Ultimate Oxygen 17.51 % by wt

5 Ultimate Oxygen 17.37 % by wt

6 Ultimate Oxygen 17.37 % by wt

7 Ultimate Oxygen 17.6 % by wt

8 Ultimate Oxygen 17.73 % by wt

9 Ultimate Oxygen 17.51 % by wt

Wednesday, February 16, 2011 Page 21 of 34
KCP&L Hawthorn Unit 5A

Sampling / Stack Data Results Detail

Location Stack - 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

Wednesday, February 16, 2011 Page 22 of 34
KCP&L Hawthorn Unit 5A

Location Stack - 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

Wednesday, February 16, 2011 Page 23 of 34
KCP&L Hawthorn Unit 5A

Location Stack - Method 26A

Average

Run Number 1 2 3

Test Date 4/22/2010 4/23/2010 4/24/2010

Run Start Time 7:34:00 PM 8:52:00 AM 7:35:00 PM

Run Finish Time 10:57:00 PM 4/24/2010 

6:59:00 PM

11:07:00 PM

Net Traversing Points 16 16 16

Net Run Time, minutes 180 180 180

Nozzle Diameter, inches 0.187 0.187 0.187 0.187

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.998 0.998 0.998 0.998

Barometric Pressure, inches of Mercury 28.77 28.79 28.41 28.657

Average Orifice Meter Differential, inches H2O 1.90 1.86 1.86 1.873

Dry Gas Meter Volume Sampled, cubic feet 138.890 139.295 128.370 135.518

Average Dry Gas Meter Temperature, °F 74.59 74.31 73.41 74.103

Dry Gas Meter Volume Sampled, dscf 132.281 132.814 120.994 128.696

Total Moisture Liquid collected, g 497.2 502.4 472.2 490.600

Volume of Water Vapor, standard cubic feet 23.40 23.65 22.23 23.093

Moisture Content of Stack Gas, % 15.03 15.12 15.52 15.223

Moisture Saturation at Stack Gas Temperature, % 61.10 61.72 59.96 60.927

Dry Mole Fraction 0.8497 0.8488 0.8448 0.848

Carbon Dioxide, % 13.8 13.5 12.5 13.267

Oxygen, % 5.7 5.7 6.9 6.100

Carbon Monoxide & Nitrogen, % 80.5 80.8 80.6 80.633

Fuel Factor 1.10 1.13 1.12

Dry Molecular Weight, lb/lb-Mole 30.44 30.39 30.28 30.370

Wet Molecular weight, lb/lb-Mole 28.57 28.52 28.37 28.487

Flue Gas Static Pressure, inches of H2O -2.1 -2.1 -2.1 -2.100

Absolute Flue Gas Pressure, inches of Mercury 28.62 28.64 28.26 28.507

Average Stack Gas Temperature, °F 186.19 186.69 184.75 185.877

Average Velocity Head, inches of H2O 2.2674033097

4881

2.227976422

56353

2.236264070

01004

2.244

Average Stack Gas Velocity, feet/second 96.13 95.38 96.30 95.937

Stack Cross-Sectional Area, square feet 323.655 323.655 323.655 323.655

Dry Volumetric Flow Rate, dry scfm 1,239,766.4 1,228,698.9 1,221,987.9 1,230,151.0

67

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,866,777.3 1,852,212.8 1,870,078.6 1,863,022.9

00

Percent Isokinetic of Sampling Rate, % 100.6 101.9 93.3 98.600

Percent Excess Air, % 36.7 36.5 48.0 40.400

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

Round Duct Diameter, inches 243.6 243.6 243.6

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 24 of 34
KCP&L Hawthorn Unit 5A

Location Stack - 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

Wednesday, February 16, 2011 Page 25 of 34
KCP&L Hawthorn Unit 5A

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 26 of 34
KCP&L Hawthorn Unit 5A

Location Stack - 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

Wednesday, February 16, 2011 Page 27 of 34
KCP&L Hawthorn Unit 5A

Location Stack - 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

Wednesday, February 16, 2011 Page 28 of 34
KCP&L Hawthorn Unit 5A

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 29 of 34
KCP&L Hawthorn Unit 5A

Location Stack - 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

Wednesday, February 16, 2011 Page 30 of 34
KCP&L Hawthorn Unit 5A

Location Stack - 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

Wednesday, February 16, 2011 Page 31 of 34
KCP&L Hawthorn Unit 5A

Location Stack - 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

Wednesday, February 16, 2011 Page 32 of 34
KCP&L Hawthorn Unit 5A

Location Stack - 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

Wednesday, February 16, 2011 Page 33 of 34
KCP&L Hawthorn Unit 5A

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 34 of 34