Name: Ms. Debi Schramm

Title: Environmental Engineer

Company: FirstEnergy Corporation

Sign Date: 9/3/2010

Name: Mr. James E. Locke

Title: Manager, Field Testing & Operation

Company: CONSOL Energy Inc.

Sign Date: 9/3/2010

Permitted Facility Representative / Date Testing Company Representative / Date

First Energy, Eastlake Station ICR

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.

Thursday, February 17, 2011 Page 1 of 29
First Energy, Eastlake Station ICR

9/3/2010

Facility Information:

FirstEnergy Corp. Eastlake Power Plant

10 Erie Road

Eastlake OH 44095

Contact: Mr. Ray Evans

Phone: 330-761-4482

Fax:

Email: rlevans@firstenergycorp.com

Testing Company:

CONSOL Energy

4000 Brownsville Road

South Park PA 15129-9545

Contact:Jim Locke

Phone: 412-854-6607

Fax: 412-854-6613

Email: jimlocke@consolenergy.com

Air Permit Number:

43-4911-895-1

Permitted Source ID/Name:

2837 3

Permitted Maximum Process Rate:

145 MW

Max. Normal Operation Process Rate:

Near Full Load

Target Process Test Rate

Near Full Load

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

 process flow diagram:

Eastlake Station is located on the shore of Lake Erie, in Eastlake, Ohio. Unit 3 is a tangential-fired 145-megawatt 

boiler that fires bituminous coal to produce steam for electricity generation. The unit is equipped with cold-side 

electrostatic precipitators for particulate emissions control and low-NOx burner technology for NOx emission control.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 10000386332 FRS #: 110010772217

SCC / Description 10100212 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Pulverized Coal: Dry Bottom (Tangential) (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

Unit 3 Stack 144 0 0 0 0 0 4 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Unit 1 Stack Carbon Monoxide Method 10 3 120 0

Unit 1 Stack Formaldehyde Method 0011 3 120 0

Total organic compounds 

(TOC) as Propane

Unit 1 Stack Method 25A 3 120 0

Unit 1 Stack Hydrogen Chloride Method 26A 3 60 0

Unit 1 Stack Hydrogen Fluoride Method 26A 3 60 0

Regulation Description Compound Limit Unit

NA 0

Thursday, February 17, 2011 Page 2 of 29
First Energy, Eastlake Station ICR

9/3/2010

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.

Unit 1 Stack Total PM2.5 OTM - 27/28 3 362 0

Unit 1 Stack Total Particulate OTM - 27/28 3 362 0

Unit 1 Stack Filterable Particulate OTM - 27/28 3 362 0

Organic Condensible 

Particulate

Unit 1 Stack OTM - 27/28 3 362 0

Inorganic (Aqueous) 

Condensible Part.

Unit 1 Stack OTM - 27/28 3 362 0

Unit 1 Stack Filterable PM2.5 OTM - 27/28 3 362 0

Unit 1 Stack Cadmium Method 29 3 240 0

Unit 1 Stack Antimony Method 29 3 240 0

Unit 1 Stack Lead Method 29 3 240 0

Unit 1 Stack Selenium Method 29 3 240 0

Unit 1 Stack Nickel Method 29 3 240 0

Unit 1 Stack Cobalt Method 29 3 240 0

Unit 1 Stack Beryllium Method 29 3 240 0

Unit 1 Stack Arsenic Method 29 3 240 0

Unit 1 Stack Filterable Particulate Method 29 3 240 0

Unit 1 Stack Chromium Method 29 3 240 0

Unit 1 Stack Manganese Method 29 3 240 0

Unit 1 Stack O2 Method 3A O2 3 120 0

Unit 1 Stack Co2 Method 3A CO2 3 120 0

Unit 1 Stack Sulfur Dioxide Method 6C 3 120 0

Unit 1 Stack Nitrogen oxides (NOx) Method 7E 3 120 0

Unit 3 Stack Carbon Monoxide Method 10 3 120 0

Unit 3 Stack Formaldehyde Method 0011 3 120 0

Total organic compounds 

(TOC) as Propane

Unit 3 Stack Method 25A 3 120 0

Unit 3 Stack Hydrogen Fluoride Method 26A 3 60 0

Unit 3 Stack Hydrogen Chloride Method 26A 3 60 0

Unit 3 Stack Filterable Particulate OTM - 27/28 3 376 0

Unit 3 Stack Total PM2.5 OTM - 27/28 3 376 0

Unit 3 Stack Total Particulate OTM - 27/28 3 376 0

Unit 3 Stack Filterable PM2.5 OTM - 27/28 3 376 0

Organic Condensible 

Particulate

Unit 3 Stack OTM - 27/28 3 376 0

Inorganic (Aqueous) 

Condensible Part.

Unit 3 Stack OTM - 27/28 3 376 0

Unit 3 Stack Arsenic Method 29 3 240 0

Unit 3 Stack Beryllium Method 29 3 240 0

Unit 3 Stack Cadmium Method 29 3 240 0

Unit 3 Stack Cobalt Method 29 3 240 0

Unit 3 Stack Chromium Method 29 3 240 0

Unit 3 Stack Manganese Method 29 3 240 0

Unit 3 Stack Nickel Method 29 3 240 0

Unit 3 Stack Lead Method 29 3 240 0

Unit 3 Stack Selenium Method 29 3 240 0

Unit 3 Stack Filterable Particulate Method 29 3 240 0

Unit 3 Stack Antimony Method 29 3 240 0

Unit 3 Stack Co2 Method 3A CO2 3 120 0

Unit 3 Stack O2 Method 3A O2 3 120 0

Unit 3 Stack Sulfur Dioxide Method 6C 3 120 0

Unit 3 Stack Nitrogen oxides (NOx) Method 7E 3 120 0

Thursday, February 17, 2011 Page 3 of 29
First Energy, Eastlake Station ICR

9/3/2010

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.

None

Thursday, February 17, 2011 Page 4 of 29
First Energy, Eastlake Station ICR

9/3/2010

Sampling / Stack Data Results Summary

Location Unit 3 Stack - Method 0011

Average

Run Number U3-M0011-1 U3-M0011-

2

U3-M0011-3

Test Date 5/27/2010 5/27/2010 5/27/2010

Run Start Time 8:34:00 AM 11:53:00 

AM

3:42:00 PM

Run Finish Time 10:24:00 AM 1:43:00 PM 5:32:00 PM

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 72.553 74.420 72.427 73.133

Moisture Content of Stack Gas, % 8.01 9.00 8.54 8.517

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

Carbon Dioxide, % 10.6 10.8 10.6 10.667

Oxygen, % 9.7 9.5 9.7 9.633

Average Stack Gas Temperature, °F 318.50 321.08 322.08 320.553

Dry Volumetric Flow Rate, dry scfm 414,755.3 427,074.9 415,469.2 419,099.800

Actual Wet Volumetric Flue Gas Flow Rate, acfm 693,035.8 723,775.6 702,196.7 706,336.033

Percent Isokinetic of Sampling Rate, % 94.3 94.0 94.0 94.100

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 Unit 3 Stack - Method 10

Average

Run Number U3-M10-1 U3-M10-2 U3-M10-3

Test Date 5/27/2010 5/27/2010 5/27/2010

Run Start Time 8:34:00 AM 11:48:00 

AM

3:40:00 PM

Run Finish Time 10:46:00 AM 1:55:00 PM 5:58:00 PM

Carbon Dioxide, % 10 10.2 10 10.067

Oxygen, % 9.3 9.2 9.4 9.300

Dry Volumetric Flow Rate, dry scfm 423247 435926 423215 427,462.667

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

Moisture, % 7.3 8.9 8.3 8.167

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Thursday, February 17, 2011 Page 5 of 29
First Energy, Eastlake Station ICR

9/3/2010

Location Unit 3 Stack - Method 25A

Average

Run Number U3-25A-1 U3-25A-2 U3-25A-3

Test Date 5/27/2010 5/27/2010 5/27/2010

Run Start Time 8:34:00 AM 11:48:00 

AM

3:40:00 PM

Run Finish Time 10:46:00 AM 1:55:00 PM 5:58:00 PM

Carbon Dioxide, % 10 10.2 10 10.067

Oxygen, % 9.3 9.2 9.4 9.300

Dry Volumetric Flow Rate, dry scfm 423247 435926 423247 427,473.333

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

Moisture, % 7.3 8.9 8.3 8.167

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Unit 3 Stack - Method 26A

Average

Run Number U3-26A-4 U3-26A-5 U3-26A-6

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

Run Start Time 8:49:00 AM 12:12:00 

PM

2:02:00 PM

Run Finish Time 9:44:00 AM 1:07:00 PM 2:57:00 PM

Net Run Time, minutes 60 60 60

Dry Gas Meter Volume Sampled, dscf 41.774 42.207 42.541 42.174

Moisture Content of Stack Gas, % 8.34 8.78 8.44 8.520

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

Carbon Dioxide, % 10.5 10.7 10.8 10.667

Oxygen, % 9.8 9.7 9.5 9.667

Average Stack Gas Temperature, °F 314.25 319.83 321.50 318.527

Dry Volumetric Flow Rate, dry scfm 413,412.8 411,202.6 413,503.6 412,706.333

Actual Wet Volumetric Flue Gas Flow Rate, acfm 690,457.2 694,325.1 697,107.3 693,963.200

Percent Isokinetic of Sampling Rate, % 96.7 98.3 98.5 97.833

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

Thursday, February 17, 2011 Page 6 of 29
First Energy, Eastlake Station ICR

9/3/2010

Location Unit 3 Stack - Method 29

Average

Run Number U3-M29-1 U3-M29-2 U3-M29-3

Test Date 5/25/2010 5/25/2010 5/26/2010

Run Start Time 10:08:00 AM 3:30:00 PM 8:17:00 AM

Run Finish Time 1:58:00 PM 7:20:00 PM 12:07:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 140.474 143.037 143.421 142.311

Moisture Content of Stack Gas, % 8.45 8.71 8.39 8.517

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

Carbon Dioxide, % 10.6 10.76 10.6 10.653

Oxygen, % 9.7 9.5 9.8 9.667

Average Stack Gas Temperature, °F 321.00 318.96 317.58 319.180

Dry Volumetric Flow Rate, dry scfm 403,133.3 412,032.9 416,944.7 410,703.633

Actual Wet Volumetric Flue Gas Flow Rate, acfm 670,846.2 686,521.4 696,089.4 684,485.667

Percent Isokinetic of Sampling Rate, % 94.0 93.6 92.8 93.467

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 Unit 3 Stack - Method 3A CO2

Average

Run Number U3-3ACO2-

1

U3-

3ACO2-2

U3-3ACO2-

3

Test Date 5/27/2010 5/27/2010 5/27/2010

Run Start Time 8:34:00 AM 11:48:00 

AM

3:40:00 PM

Run Finish Time 10:46:00 AM 1:55:00 PM 5:58:00 PM

Carbon Dioxide, % 10 10.2 10 10.067

Oxygen, % 9.3 9.2 9.4 9.300

Dry Volumetric Flow Rate, dry scfm 423247 435926 423215 427,462.667

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

Moisture, % 7.3 8.9 8.3 8.167

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Thursday, February 17, 2011 Page 7 of 29
First Energy, Eastlake Station ICR

9/3/2010

Location Unit 3 Stack - Method 3A O2

Average

Run Number U3-3AO2-1 U3-3AO2-

2

U3-3AO2-3

Test Date 5/27/2010 5/27/2010 5/27/2010

Run Start Time 8:34:00 AM 11:48:00 

AM

3:40:00 PM

Run Finish Time 10:46:00 AM 1:55:00 PM 5:58:00 PM

Carbon Dioxide, % 10 10.2 10 10.067

Oxygen, % 9.3 9.2 9.4 9.300

Dry Volumetric Flow Rate, dry scfm 423247 435926 423215 427,462.667

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

Moisture, % 7.3 8.9 8.3 8.167

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Unit 3 Stack - Method 6C

Average

Run Number U3-6C-1 U3-6C-2 U3-6C-3

Test Date 5/27/2010 5/27/2010 5/27/2010

Run Start Time 8:34:00 AM 11:48:00 

AM

3:40:00 PM

Run Finish Time 10:46:00 AM 1:55:00 PM 5:58:00 PM

Carbon Dioxide, % 10 10.2 10 10.067

Oxygen, % 9.3 9.2 9.4 9.300

Dry Volumetric Flow Rate, dry scfm 423247 435926 423215 427,462.667

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

Moisture, % 7.3 8.9 8.3 8.167

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Thursday, February 17, 2011 Page 8 of 29
First Energy, Eastlake Station ICR

9/3/2010

Location Unit 3 Stack - Method 7E

Average

Run Number U3-7E-1 U3-7E-2 U3-7E-3

Test Date 5/27/2010 5/27/2010 5/27/2010

Run Start Time 8:34:00 AM 11:48:00 

AM

3:40:00 PM

Run Finish Time 10:46:00 AM 1:55:00 PM 5:58:00 PM

Carbon Dioxide, % 10 10.2 10 10.067

Oxygen, % 9.3 9.2 9.4 9.300

Dry Volumetric Flow Rate, dry scfm 423247 435926 423215 427,462.667

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

Moisture, % 7.3 8.9 8.3 8.167

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Unit 3 Stack - OTM - 27/28

Average

Run Number 1 2 3

Test Date 5/25/2010 5/26/2010 5/26/2010

Run Start Time

Run Finish Time

Net Run Time, minutes 343.25 371.5 375.5

Dry Gas Meter Volume Sampled, dscf 126.011 136.220 137.394 133.208

Moisture Content of Stack Gas, % 6.47 7.90 8.22 7.530

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

Carbon Dioxide, % 10.5 10.5 10.5 10.500

Oxygen, % 9 9 9 9.000

Average Stack Gas Temperature, °F 312.33 311.25 317.42 313.667

Dry Volumetric Flow Rate, dry scfm 408,724.0 416,079.7 416,677.6 413,827.100

Actual Wet Volumetric Flue Gas Flow Rate, acfm 658,360.3 682,246.3 694,935.8 678,514.133

Percent Isokinetic of Sampling Rate, % 108.5 106.5 106.1 107.033

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

Thursday, February 17, 2011 Page 9 of 29
First Energy, Eastlake Station ICR

9/3/2010

Emissions Summary

Location: Unit 3 Stack - Method 0011

Compound: Formaldehyde

Average

RunNumber U3-M0011-1 U3-M0011-2 U3-M0011-3

Mass_mg 0.013 0.014 0.008 0.012

Elb/hr 9.83E-03 1.06E-02 6.07E-03 0.009

gr/dscf 2.77E-06 2.90E-06 1.70E-06 0.000

lb/mmBtuO2 7.21E-06 7.44E-06 4.44E-06 0.000

mg/dscm 6.33E-03 6.64E-03 3.90E-03 0.006

ppm 5.07E-03 5.32E-03 3.12E-03 0.005

Location: Unit 3 Stack - Method 10

Compound: Carbon Monoxide

Average

Run U3-M10-1 U3-M10-2 U3-M10-3

Elb/hr 4.59E+01 4.83E+01 4.51E+01 46.433

gr/dscf 1.27E-02 1.29E-02 1.24E-02 0.013

lb/mmBtuO2 3.19E-02 3.22E-02 3.16E-02 0.032

mg/dscm 2.90E+01 2.96E+01 2.85E+01 29.033

ppm 2.49E+01 2.54E+01 2.44E+01 24.900

Location: Unit 3 Stack - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run U3-25A-1 U3-25A-2 U3-25A-3

Elb/hr 3.17E-01 9.58E-03 4.81E-01 0.269

gr/dscf 8.73E-05 2.56E-06 1.33E-04 0.000

lb/mmBtuO2 2.20E-04 6.40E-06 3.36E-04 0.000

mg/dscm 2.00E-01 5.87E-03 3.03E-01 0.170

ppm 1.09E-01 3.20E-03 1.65E-01 0.092

Location: Unit 3 Stack - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber U3-26A-4 U3-26A-5 U3-26A-6

Mass_mg 65.7117 66.939 68.2535 66.968

Elb/hr 8.60E+01 8.63E+01 8.78E+01 86.700

gr/dscf 2.43E-02 2.45E-02 2.48E-02 0.025

lb/mmBtuO2 6.39E-02 6.38E-02 6.34E-02 0.064

mg/dscm 5.56E+01 5.60E+01 5.67E+01 56.100

ppm 3.66E+01 3.69E+01 3.74E+01 36.967

Compound: Hydrogen Fluoride

Average

RunNumber U3-26A-4 U3-26A-5 U3-26A-6

Mass_mg 4.3613 4.9396 4.7679 4.690

Elb/hr 5.71E+00 6.37E+00 6.13E+00 6.070

gr/dscf 1.61E-03 1.81E-03 1.73E-03 0.002

lb/mmBtuO2 4.24E-03 4.71E-03 4.43E-03 0.004

mg/dscm 3.69E+00 4.13E+00 3.96E+00 3.927

Thursday, February 17, 2011 Page 10 of 29
First Energy, Eastlake Station ICR

9/3/2010

ppm 4.43E+00 4.97E+00 4.76E+00 4.720

Location: Unit 3 Stack - Method 29

Compound: Antimony

Average

RunNumber U3-M29-1 U3-M29-2 U3-M29-3

Mass_mg 0.000178 0.0001567 0.0001512 0.000

Elb/hr 6.76E-05 5.97E-05 5.81E-05 0.000

gr/dscf 1.96E-08 1.69E-08 1.63E-08 0.000

lb/mmBtuO2 5.10E-08 4.33E-08 4.28E-08 0.000

mg/dscm 4.48E-05 3.87E-05 3.72E-05 0.000

ppm 8.84E-06 7.64E-06 7.36E-06 0.000

Compound: Arsenic

Average

RunNumber U3-M29-1 U3-M29-2 U3-M29-3

Mass_mg 0.0023053 0.0023347 0.0023738 0.002

Elb/hr 8.75E-04 8.90E-04 9.13E-04 0.001

gr/dscf 2.53E-07 2.52E-07 2.55E-07 0.000

lb/mmBtuO2 6.60E-07 6.45E-07 6.72E-07 0.000

mg/dscm 5.80E-04 5.77E-04 5.85E-04 0.001

ppm 1.86E-04 1.85E-04 1.88E-04 0.000

Compound: Beryllium

Average

RunNumber U3-M29-1 U3-M29-2 U3-M29-3

Mass_mg 0.0000833 0.0000766 0.0000788 0.000

Elb/hr 3.16E-05 2.92E-05 3.03E-05 0.000

gr/dscf 9.15E-09 8.26E-09 8.48E-09 0.000

lb/mmBtuO2 2.39E-08 2.12E-08 2.23E-08 0.000

mg/dscm 2.09E-05 1.89E-05 1.94E-05 0.000

ppm 5.59E-05 5.05E-05 5.18E-05 0.000

Compound: Cadmium

Average

RunNumber U3-M29-1 U3-M29-2 U3-M29-3

Mass_mg 0.0003259 0.00029276 0.00012075 0.000

Elb/hr 1.24E-04 1.12E-04 4.64E-05 0.000

gr/dscf 3.58E-08 3.16E-08 1.30E-08 0.000

lb/mmBtuO2 9.33E-08 8.09E-08 3.42E-08 0.000

mg/dscm 8.19E-05 7.23E-05 2.97E-05 0.000

ppm 1.75E-05 1.55E-05 6.36E-06 0.000

Compound: Chromium

Average

RunNumber U3-M29-1 U3-M29-2 U3-M29-3

Mass_mg 0.014734 0.032417 0.036604 0.028

Elb/hr 5.59E-03 1.24E-02 1.41E-02 0.011

gr/dscf 1.62E-06 3.50E-06 3.94E-06 0.000

lb/mmBtuO2 4.22E-06 8.96E-06 1.04E-05 0.000

mg/dscm 3.70E-03 8.00E-03 9.01E-03 0.007

ppm 1.71E-03 3.70E-03 4.17E-03 0.003

Thursday, February 17, 2011 Page 11 of 29
First Energy, Eastlake Station ICR

9/3/2010

Process Run Data

Compound: Cobalt

Average

RunNumber U3-M29-1 U3-M29-2 U3-M29-3

Mass_mg 0.0012088 0.002124 0.0009114 0.001

Elb/hr 4.59E-04 8.09E-04 3.50E-04 0.001

gr/dscf 1.33E-07 2.29E-07 9.81E-08 0.000

lb/mmBtuO2 3.46E-07 5.87E-07 2.58E-07 0.000

mg/dscm 3.04E-04 5.24E-04 2.24E-04 0.000

ppm 1.24E-04 2.14E-04 9.16E-05 0.000

Compound: Filterable Particulate

Average

RunNumber U3-M29-1 U3-M29-2 U3-M29-3

Mass_mg 21.35 17.15 20.45 19.650

Elb/hr 8.10E+00 6.53E+00 7.86E+00 7.497

gr/dscf 2.35E-03 1.85E-03 2.20E-03 0.002

lb/mmBtuO2 6.12E-03 4.74E-03 5.79E-03 0.006

mg/dscm 5.37E+00 4.23E+00 5.04E+00 4.880

ppm #Num!

Thursday, February 17, 2011 Page 12 of 29
First Energy, Eastlake Station ICR

9/3/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Coal Firing Rate 92 thousand lbs per hr 5/18/10 - Unit 1 

M29 Run 1

0

10 Coal Firing Rate 90.7 thousand lbs per hr 5/19/10 - Unit 1 

M29 Runs 2-3, 

M0011 Runs 1-2

0

11 Coal Firing Rate 88.9 thousand lbs per hr 5/20/10 - Unit 1 

M0031 Runs 1-3, 

M0010 Runs 1-3, 

M0011 Run 3

0

12 Coal Firing Rate 86 thousand lbs per hr 5/24/10 - Unit 1 

M26A Runs 1-3, 

M3A, 6C, 7E, 10, 

18, 25A Runs 1-3

0

2 Coal Firing Rate 80.9 thousand lbs per hr 6/30/10 - Unit 1 

CTM033 Runs 1-3

0

3 Coal Firing Rate 81.2 thousand lbs per hr 7/14/10 - 30B 

Runs 1-3

0

4 Coal Firing Rate 68.9 thousand lbs per hr 5/25/10 - Unit 3 

M29 Runs 1-2

0

5 Coal Firing Rate 70.9 thousand lbs per hr 5/26/10 - M29 

Run 3

0

6 Coal Firing Rate 74 thousand lbs per hr 5/27/10 - M0031 

Runs 1-3, M0010 

Runs 1-3, M0011 

Runs 1-3, M3a, 

6C, 7E, 10, 18, 

25A Runs 1-3

0

7 Coal Firing Rate 91.1 thousand lbs per hr 6/16/10 - CTM033 

Runs 1-3, M26A 

Runs 4-6

0

8 Coal Firing Rate 92.2 thousand lbs per hr 7/15/10 - 30B 

Runs 1-3

0

1 Average Heat Input 936 mmBtu/hr 5/18/10 - Unit 1 

M29 Run 1

0

10 Average Heat Input 933 mmBtu/hr 5/19/10 - Unit 1 

M29 Runs 2-3, 

M0011 Runs 1-2

0

11 Average Heat Input 897 mmBtu/hr 5/20/10 - Unit 1 

M0031 Runs 1-3, 

M0010 Runs 1-3, 

M0011 Run 3

0

12 Average Heat Input 1097 mmBtu/hr 5/24/10 - Unit 1 

M26A Runs 1-3, 

M3A, 6C, 7E, 10, 

18, 25A Runs 1-3

0

Thursday, February 17, 2011 Page 13 of 29
First Energy, Eastlake Station ICR

9/3/2010

2 Average Heat Input 986 mmBtu/hr 6/30/10 - Unit 1 

CTM033 Runs 1-3

0

3 Average Heat Input 1075 mmBtu/hr 7/14/10 - 30B 

Runs 1-3

0

4 Average Heat Input 981 mmBtu/hr 5/25/10 - Unit 3 

M29 Runs 1-2

0

5 Average Heat Input 1018 mmBtu/hr 5/26/10 - M29 

Run 3

0

6 Average Heat Input 968 mmBtu/hr 5/27/10 - M0031 

Runs 1-3, M0010 

Runs 1-3, M0011 

Runs 1-3, M3a, 

6C, 7E, 10, 18, 

25A Runs 1-3

0

7 Average Heat Input 1021 mmBtu/hr 6/16/10 - CTM033 

Runs 1-3, M26A 

Runs 4-6

0

8 Average Heat Input 1010 mmBtu/hr 7/15/10 - 30B 

Runs 1-3

0

1 Steam Output 691Thousand pounds per hour 5/18/10 - Unit 1 

M29 Run 1

0

10 Steam Output 685Thousand pounds per hour 5/19/10 - Unit 1 

M29 Runs 2-3, 

M0011 Runs 1-2

0

11 Steam Output 666Thousand pounds per hour 5/20/10 - Unit 1 

M0031 Runs 1-3, 

M0010 Runs 1-3, 

M0011 Run 3

0

12 Steam Output 837Thousand pounds per hour 5/24/10 - Unit 1 

M26A Runs 1-3, 

M3A, 6C, 7E, 10, 

18, 25A Runs 1-3

0

2 Steam Output 682Thousand pounds per hour 6/30/10 - Unit 1 

CTM033 Runs 1-3

0

3 Steam Output 775Thousand pounds per hour 7/14/10 - 30B 

Runs 1-3

0

4 Steam Output 749Thousand pounds per hour 5/25/10 - Unit 3 

M29 Runs 1-2

0

5 Steam Output 787Thousand pounds per hour 5/26/10 - M29 

Run 3

0

6 Steam Output 745Thousand pounds per hour 5/27/10 - M0031 

Runs 1-3, M0010 

Runs 1-3, M0011 

Runs 1-3, M3a, 

6C, 7E, 10, 18, 

25A Runs 1-3

0

7 Steam Output 775Thousand pounds per hour 6/16/10 - CTM033 

Runs 1-3, M26A 

Runs 4-6

0

Thursday, February 17, 2011 Page 14 of 29
First Energy, Eastlake Station ICR

9/3/2010

8 Steam Output 789Thousand pounds per hour 7/15/10 - 30B 

Runs 1-3

0

1 Net Generation 2249 MWh 5/18/10 - Unit 1 

M29 Run 1

0

10 Net Generation 2241 MWh 5/19/10 - Unit 1 

M29 Runs 2-3, 

M0011 Runs 1-2

0

11 Net Generation 2165 MWh 5/20/10 - Unit 1 

M0031 Runs 1-3, 

M0010 Runs 1-3, 

M0011 Run 3

0

12 Net Generation 2662 MWh 5/24/10 - Unit 1 

M26A Runs 1-3, 

M3A, 6C, 7E, 10, 

18, 25A Runs 1-3

0

2 Net Generation 2190 MWh 6/30/10 - Unit 1 

CTM033 Runs 1-3

0

3 Net Generation 2427 MWh 7/14/10 - 30B 

Runs 1-3

0

4 Net Generation 2429 MWh 5/25/10 - Unit 3 

M29 Runs 1-2

0

5 Net Generation 2545 MWh 5/26/10 - M29 

Run 3

0

6 Net Generation 2390 MWh 5/27/10 - M0031 

Runs 1-3, M0010 

Runs 1-3, M0011 

Runs 1-3, M3a, 

6C, 7E, 10, 18, 

25A Runs 1-3

0

7 Net Generation 2501 MWh 6/16/10 - CTM033 

Runs 1-3, M26A 

Runs 4-6

0

8 Net Generation 2491 MWh 7/15/10 - 30B 

Runs 1-3

0

1 Gross Generation 103.1 MWh 5/18/10 - Unit 1 

M29 Run 1

0

10 Gross Generation 102.7 MWh 5/19/10 - Unit 1 

M29 Runs 2-3, 

M0011 Runs 1-2

0

11 Gross Generation 99.4 MWh 5/20/10 - Unit 1 

M0031 Runs 1-3, 

M0010 Runs 1-3, 

M0011 Run 3

0

12 Gross Generation 121 MWh 5/24/10 - Unit 1 

M26A Runs 1-3, 

M3A, 6C, 7E, 10, 

18, 25A Runs 1-3

0

2 Gross Generation 101 MWh 6/30/10 - Unit 1 

CTM033 Runs 1-3

0

Thursday, February 17, 2011 Page 15 of 29
First Energy, Eastlake Station ICR

9/3/2010

3 Gross Generation 111.6 MWh 7/14/10 - 30B 

Runs 1-3

0

4 Gross Generation 111.2 MWh 5/25/10 - Unit 3 

M29 Runs 1-2

0

5 Gross Generation 116.2 MWh 5/26/10 - M29 

Run 3

0

6 Gross Generation 109.7 MWh 5/27/10 - M0031 

Runs 1-3, M0010 

Runs 1-3, M0011 

Runs 1-3, M3a, 

6C, 7E, 10, 18, 

25A Runs 1-3

0

7 Gross Generation 114.2 MWh 6/16/10 - CTM033 

Runs 1-3, M26A 

Runs 4-6

0

8 Gross Generation 114.6 MWh 7/15/10 - 30B 

Runs 1-3

0

1 Flue Gas Flow Rate 325000 dscfm 5/18/10 - Unit 1 

M29 Run 1

0

10 Flue Gas Flow Rate 324000 dscfm 5/19/10 - Unit 1 

M29 Runs 2-3, 

M0011 Runs 1-2

0

11 Flue Gas Flow Rate 317000 dscfm 5/20/10 - Unit 1 

M0031 Runs 1-3, 

M0010 Runs 1-3, 

M0011 Run 3

0

12 Flue Gas Flow Rate 350000 dscfm 5/24/10 - Unit 1 

M26A Runs 1-3, 

M3A, 6C, 7E, 10, 

18, 25A Runs 1-3

0

2 Flue Gas Flow Rate 332000 dscfm 6/30/10 - Unit 1 

CTM033 Runs 1-3

0

3 Flue Gas Flow Rate 341000 dscfm 7/14/10 - 30B 

Runs 1-3

0

4 Flue Gas Flow Rate 337000 dscfm 5/25/10 - Unit 3 

M29 Runs 1-2

0

5 Flue Gas Flow Rate 348000 dscfm 5/26/10 - M29 

Run 3

0

6 Flue Gas Flow Rate 333000 dscfm 5/27/10 - M0031 

Runs 1-3, M0010 

Runs 1-3, M0011 

Runs 1-3, M3a, 

6C, 7E, 10, 18, 

25A Runs 1-3

0

7 Flue Gas Flow Rate 349000 dscfm 6/16/10 - CTM033 

Runs 1-3, M26A 

Runs 4-6

0

8 Flue Gas Flow Rate 348000 dscfm 7/15/10 - 30B 

Runs 1-3

0

Thursday, February 17, 2011 Page 16 of 29
First Energy, Eastlake Station ICR

9/3/2010

1 Flue Gas Sampling Point Temperature 342.1 deg. F 5/18/10 - Unit 1 

M29 Run 1

0

10 Flue Gas Sampling Point Temperature 344.7 deg. F 5/19/10 - Unit 1 

M29 Runs 2-3, 

M0011 Runs 1-2

0

11 Flue Gas Sampling Point Temperature 349.2 deg. F 5/20/10 - Unit 1 

M0031 Runs 1-3, 

M0010 Runs 1-3, 

M0011 Run 3

0

12 Flue Gas Sampling Point Temperature 345.8 deg. F 5/24/10 - Unit 1 

M26A Runs 1-3, 

M3A, 6C, 7E, 10, 

18, 25A Runs 1-3

0

2 Flue Gas Sampling Point Temperature 345.9 deg. F 6/30/10 - Unit 1 

CTM033 Runs 1-3

0

3 Flue Gas Sampling Point Temperature 351.6 deg. F 7/14/10 - 30B 

Runs 1-3

0

4 Flue Gas Sampling Point Temperature 318.8 deg. F 5/25/10 - Unit 3 

M29 Runs 1-2

0

5 Flue Gas Sampling Point Temperature 318.1 deg. F 5/26/10 - M29 

Run 3

0

6 Flue Gas Sampling Point Temperature 318.4 deg. F 5/27/10 - M0031 

Runs 1-3, M0010 

Runs 1-3, M0011 

Runs 1-3, M3a, 

6C, 7E, 10, 18, 

25A Runs 1-3

0

7 Flue Gas Sampling Point Temperature 325.1 deg. F 6/16/10 - CTM033 

Runs 1-3, M26A 

Runs 4-6

0

8 Flue Gas Sampling Point Temperature 333 deg. F 7/15/10 - 30B 

Runs 1-3

0

1 Flue Gas Oxygen Content 4.02 % 5/18/10 - Unit 1 

M29 Run 1

0

10 Flue Gas Oxygen Content 4.15 % 5/19/10 - Unit 1 

M29 Runs 2-3, 

M0011 Runs 1-2

0

11 Flue Gas Oxygen Content 4.17 % 5/20/10 - Unit 1 

M0031 Runs 1-3, 

M0010 Runs 1-3, 

M0011 Run 3

0

12 Flue Gas Oxygen Content 3.63 % 5/24/10 - Unit 1 

M26A Runs 1-3, 

M3A, 6C, 7E, 10, 

18, 25A Runs 1-3

0

2 Flue Gas Oxygen Content 4.4 % 6/30/10 - Unit 1 

CTM033 Runs 1-3

0

3 Flue Gas Oxygen Content 3.81 % 7/14/10 - 30B 

Runs 1-3

0

Thursday, February 17, 2011 Page 17 of 29
First Energy, Eastlake Station ICR

9/3/2010

APCD Run Data

4 Flue Gas Oxygen Content 4.35 % 5/25/10 - Unit 3 

M29 Runs 1-2

0

5 Flue Gas Oxygen Content 4.17 % 5/26/10 - M29 

Run 3

0

6 Flue Gas Oxygen Content 4.32 % 5/27/10 - M0031 

Runs 1-3, M0010 

Runs 1-3, M0011 

Runs 1-3, M3a, 

6C, 7E, 10, 18, 

25A Runs 1-3

0

7 Flue Gas Oxygen Content 3.77 % 6/16/10 - CTM033 

Runs 1-3, M26A 

Runs 4-6

0

8 Flue Gas Oxygen Content 3.84 % 7/15/10 - 30B 

Runs 1-3

0

1 Flue Gas Carbon Dioxide Content 8.75 % 5/18/10 - Unit 1 

M29 Run 1

0

10 Flue Gas Carbon Dioxide Content 8.65 % 5/19/10 - Unit 1 

M29 Runs 2-3, 

M0011 Runs 1-2

0

11 Flue Gas Carbon Dioxide Content 8.57 % 5/20/10 - Unit 1 

M0031 Runs 1-3, 

M0010 Runs 1-3, 

M0011 Run 3

0

12 Flue Gas Carbon Dioxide Content 9.44 % 5/24/10 - Unit 1 

M26A Runs 1-3, 

M3A, 6C, 7E, 10, 

18, 25A Runs 1-3

0

2 Flue Gas Carbon Dioxide Content 8.97 % 6/30/10 - Unit 1 

CTM033 Runs 1-3

0

3 Flue Gas Carbon Dioxide Content 9.42 % 7/14/10 - 30B 

Runs 1-3

0

4 Flue Gas Carbon Dioxide Content 8.76 % 5/25/10 - Unit 3 

M29 Runs 1-2

0

5 Flue Gas Carbon Dioxide Content 8.76 % 5/26/10 - M29 

Run 3

0

6 Flue Gas Carbon Dioxide Content 8.74 % 5/27/10 - M0031 

Runs 1-3, M0010 

Runs 1-3, M0011 

Runs 1-3, M3a, 

6C, 7E, 10, 18, 

25A Runs 1-3

0

7 Flue Gas Carbon Dioxide Content 8.79 % 6/16/10 - CTM033 

Runs 1-3, M26A 

Runs 4-6

0

8 Flue Gas Carbon Dioxide Content 8.84 % 7/15/10 - 30B 

Runs 1-3

0

Thursday, February 17, 2011 Page 18 of 29
First Energy, Eastlake Station ICR

9/3/2010

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 LOW NOX BURNERS 0 0

1 ELECTROSTATIC PRECIPITATOR 0 0

Thursday, February 17, 2011 Page 19 of 29
First Energy, Eastlake Station ICR

9/3/2010

Sampling / Stack Data Results Detail

Location Unit 3 Stack - Method 0011

Average

Run Number U3-M0011-1 U3-M0011-2 U3-M0011-3

Test Date 5/27/2010 5/27/2010 5/27/2010

Run Start Time 8:34:00 AM 11:53:00 AM 3:42:00 PM

Run Finish Time 10:24:00 AM 1:43:00 PM 5:32:00 PM

Net Traversing Points 13 13 13

Net Run Time, minutes 120 120 120

Nozzle Diameter, inches 0.179 0.179 0.179 0.179

Pitot Tube Coefficient 0.859 0.858 0.858 0.858

Dry Gas Meter Calibration Factor 0.972 0.958 0.958 0.963

Barometric Pressure, inches of Mercury 28.94 28.94 28.91 28.930

Average Orifice Meter Differential, inches H2O 1.40 1.52 1.43 1.450

Dry Gas Meter Volume Sampled, cubic feet 83.900 87.170 85.220 85.430

Average Dry Gas Meter Temperature, °F 116.08 115.29 117.17 116.180

Dry Gas Meter Volume Sampled, dscf 72.553 74.420 72.427 73.133

Total Moisture Liquid collected, g 134.3 156.4 143.7 144.800

Volume of Water Vapor, standard cubic feet 6.32 7.36 6.76 6.813

Moisture Content of Stack Gas, % 8.01 9.00 8.54 8.517

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

Dry Mole Fraction 0.9199 0.91 0.9146 0.915

Carbon Dioxide, % 10.6 10.8 10.6 10.667

Oxygen, % 9.7 9.5 9.7 9.633

Carbon Monoxide & Nitrogen, % 79.7 79.7 79.7 79.700

Fuel Factor 1.06 1.06 1.06

Dry Molecular Weight, lb/lb-Mole 30.08 30.11 30.08 30.090

Wet Molecular weight, lb/lb-Mole 29.11 29.02 29.05 29.060

Flue Gas Static Pressure, inches of H2O -3.3 -3.3 -3.3 -3.300

Absolute Flue Gas Pressure, inches of Mercury 28.70 28.70 28.67 28.690

Average Stack Gas Temperature, °F 318.50 321.08 322.08 320.553

Average Velocity Head, inches of H2O 2.0758309032

1747

2.254500332

72977

2.119567801

94218

2.150

Average Stack Gas Velocity, feet/second 102.13 106.66 103.48 104.090

Stack Cross-Sectional Area, square feet 113.097 113.097 113.097 113.097

Dry Volumetric Flow Rate, dry scfm 414,755.3 427,074.9 415,469.2 419,099.800

Actual Wet Volumetric Flue Gas Flow Rate, acfm 693,035.8 723,775.6 702,196.7 706,336.033

Percent Isokinetic of Sampling Rate, % 94.3 94.0 94.0 94.100

Percent Excess Air, % 85.5 82.3 85.5 84.433

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

Round Duct Diameter, inches 144 144 144

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

Thursday, February 17, 2011 Page 20 of 29
First Energy, Eastlake Station ICR

9/3/2010

Location Unit 3 Stack - Method 10

Average

Run Number U3-M10-1 U3-M10-2 U3-M10-3

Test Date 5/27/2010 5/27/2010 5/27/2010

Run Start Time 8:34:00 AM 11:48:00 AM 3:40:00 PM

Run Finish Time 10:46:00 AM 1:55:00 PM 5:58:00 PM

Carbon Dioxide, % 10 10.2 10 10.067

Oxygen, % 9.3 9.2 9.4 9.300

Fuel Factor 1.16 1.15 1.15

Dry Volumetric Flow Rate, dry scfm 423247 435926 423215 427,462.667

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

Moisture, % 7.3 8.9 8.3 8.167

Analyzer Make California 

Analytical 

Instruments

California 

Analytical 

Instruments

California 

Analytical 

Instruments

Analyzer Model Model 602P Model 602P Model 602P

Analyzer Serial Number

Operating Range 100 100 100 100.000

Operating Units ppm ppm ppm

No. Readings/Avg. 60 60 60 60.000

Calibration Set 2 2 2 2.000

Calibration Pre Zero Cylinder ID EB0012998-

N2

EB0012998-

N2

EB0012998-

N2

Calibration Pre Zero Cylinder Instrument Response 4.4 0 2.2 2.200

Calibration Pre Zero Cylinder Bias 4.2 -0.2 2 2.000

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID XL001279BCOXL001279BCOXL001279BCO

Calibration Pre High Cylinder Instrument Response 35.5 29.8 31.6 32.300

Calibration Pre High Cylinder Bias 4.9 -0.8 1 1.700

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB0012998-

N2

EB0012998-

N2

EB0012998-

N2

Calibration Post Zero Cylinder Instrument Response 0 2.2 4.7 2.300

Calibration Post Zero Cylinder Bias -0.2 2 4.5 2.100

Calibration Post Zero Cylinder Drift 4.4 2.2 2.5 3.033

Calibration Post High Cylinder ID XL001279BCOXL001279BCOXL001279BCO

Calibration Post High Cylinder Instrument Response 29.8 31.6 36.4 32.600

Calibration Post High Cylinder Bias -0.8 1 5.8 2.000

Calibration Post High Cylinder Drift 5.7 1.8 4.8 4.100

Cavg 26.9 25.6 27.8 26.767

Cavg Units ppmvd ppmvd ppmvd

Cgas 24.8703 25.3774 24.4377 24.895

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Thursday, February 17, 2011 Page 21 of 29
First Energy, Eastlake Station ICR

9/3/2010

Location Unit 3 Stack - Method 25A

Average

Run Number U3-25A-1 U3-25A-2 U3-25A-3

Test Date 5/27/2010 5/27/2010 5/27/2010

Run Start Time 8:34:00 AM 11:48:00 AM 3:40:00 PM

Run Finish Time 10:46:00 AM 1:55:00 PM 5:58:00 PM

Carbon Dioxide, % 10 10.2 10 10.067

Oxygen, % 9.3 9.2 9.4 9.300

Fuel Factor 1.16 1.15 1.15

Dry Volumetric Flow Rate, dry scfm 423247 435926 423247 427,473.333

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

Moisture, % 7.3 8.9 8.3 8.167

Analyzer Make JUM 

Engineering

JUM 

Engineering

JUM 

Engineering

Analyzer Model Model VE-7 Model VE-7 Model VE-7

Analyzer Serial Number

Operating Range 10 10 10 10.000

Operating Units ppm ppm ppm

No. Readings/Avg. 60 60 60 60.000

Calibration Set 5 5 5 5.000

Calibration Pre Zero Cylinder ID VOC Free Air VOC Free 

Air

VOC Free Air

Calibration Pre Zero Cylinder Instrument Response 0.2 0.2 -0.2 0.067

Calibration Pre Zero Cylinder Bias 2 2 -2 0.667

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID ALM027314-

VOC

ALM027314

-VOC

ALM027314-

VOC

Calibration Pre High Cylinder Instrument Response 5.5 5.2 5.4 5.367

Calibration Pre High Cylinder Bias 3 0 2 1.667

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID VOC Free Air VOC Free 

Air

VOC Free Air

Calibration Post Zero Cylinder Instrument Response 0.2 -0.2 -0.1 -0.033

Calibration Post Zero Cylinder Bias 2 -2 -1 -0.333

Calibration Post Zero Cylinder Drift 0 4 1 1.667

Calibration Post High Cylinder ID ALM027314-

VOC

ALM027314

-VOC

ALM027314-

VOC

Calibration Post High Cylinder Instrument Response 5.2 5.4 5 5.200

Calibration Post High Cylinder Bias 0 2 -2 0.000

Calibration Post High Cylinder Drift 3 2 4 3.000

Cavg 0.3 0.003 0.006 0.103

Cavg Units ppmvw ppmvw ppmvw

Cgas 0.1089 0.0032 0.1654 0.093

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0.1009708737

86408

2.943396226

41509E-03

0.151626168

224299

0.085

Cgasw Units ppmvw ppmvw ppmvw

Thursday, February 17, 2011 Page 22 of 29
First Energy, Eastlake Station ICR

9/3/2010

Location Unit 3 Stack - Method 26A

Average

Run Number U3-26A-4 U3-26A-5 U3-26A-6

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

Run Start Time 8:49:00 AM 12:12:00 PM 2:02:00 PM

Run Finish Time 9:44:00 AM 1:07:00 PM 2:57:00 PM

Net Traversing Points 13 13 13

Net Run Time, minutes 60 60 60

Nozzle Diameter, inches 0.19 0.19 0.19 0.190

Pitot Tube Coefficient 0.857 0.857 0.857 0.857

Dry Gas Meter Calibration Factor 0.955 0.955 0.955 0.955

Barometric Pressure, inches of Mercury 28.9 28.93 28.93 28.920

Average Orifice Meter Differential, inches H2O 2.01 2.02 2.04 2.023

Dry Gas Meter Volume Sampled, cubic feet 49.120 48.830 49.120 49.023

Average Dry Gas Meter Temperature, °F 115.63 106.96 105.88 109.490

Dry Gas Meter Volume Sampled, dscf 41.774 42.207 42.541 42.174

Total Moisture Liquid collected, g 80.8 86.3 83.3 83.467

Volume of Water Vapor, standard cubic feet 3.80 4.06 3.92 3.927

Moisture Content of Stack Gas, % 8.34 8.78 8.44 8.520

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

Dry Mole Fraction 0.9166 0.9122 0.9156 0.915

Carbon Dioxide, % 10.5 10.7 10.8 10.667

Oxygen, % 9.8 9.7 9.5 9.667

Carbon Monoxide & Nitrogen, % 79.7 79.6 79.7 79.667

Fuel Factor 1.06 1.05 1.06

Dry Molecular Weight, lb/lb-Mole 30.07 30.10 30.11 30.093

Wet Molecular weight, lb/lb-Mole 29.06 29.04 29.09 29.063

Flue Gas Static Pressure, inches of H2O -3.3 -3.3 -3.3 -3.300

Absolute Flue Gas Pressure, inches of Mercury 28.66 28.69 28.69 28.680

Average Stack Gas Temperature, °F 314.25 319.83 321.50 318.527

Average Velocity Head, inches of H2O 2.0748096861

8455

2.083894327

97925

2.099792651

70581

2.086

Average Stack Gas Velocity, feet/second 101.75 102.32 102.73 102.267

Stack Cross-Sectional Area, square feet 113.097 113.097 113.097 113.097

Dry Volumetric Flow Rate, dry scfm 413,412.8 411,202.6 413,503.6 412,706.333

Actual Wet Volumetric Flue Gas Flow Rate, acfm 690,457.2 694,325.1 697,107.3 693,963.200

Percent Isokinetic of Sampling Rate, % 96.7 98.3 98.5 97.833

Percent Excess Air, % 87.2 85.7 82.3 85.067

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

Round Duct Diameter, inches 144 144 144

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

Thursday, February 17, 2011 Page 23 of 29
First Energy, Eastlake Station ICR

9/3/2010

Location Unit 3 Stack - Method 29

Average

Run Number U3-M29-1 U3-M29-2 U3-M29-3

Test Date 5/25/2010 5/25/2010 5/26/2010

Run Start Time 10:08:00 AM 3:30:00 PM 8:17:00 AM

Run Finish Time 1:58:00 PM 7:20:00 PM 12:07:00 PM

Net Traversing Points 25 25 25

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.179 0.179 0.179 0.179

Pitot Tube Coefficient 0.858 0.858 0.858 0.858

Dry Gas Meter Calibration Factor 0.958 0.958 0.958 0.958

Barometric Pressure, inches of Mercury 29.21 29.18 28.97 29.120

Average Orifice Meter Differential, inches H2O 1.31 1.37 1.40 1.360

Dry Gas Meter Volume Sampled, cubic feet 163.330 166.010 167.870 165.737

Average Dry Gas Meter Temperature, °F 116.06 114.52 115.29 115.290

Dry Gas Meter Volume Sampled, dscf 140.474 143.037 143.421 142.311

Total Moisture Liquid collected, g 275.6 290 278.9 281.500

Volume of Water Vapor, standard cubic feet 12.97 13.65 13.13 13.250

Moisture Content of Stack Gas, % 8.45 8.71 8.39 8.517

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

Dry Mole Fraction 0.9155 0.9129 0.9161 0.915

Carbon Dioxide, % 10.6 10.76 10.6 10.653

Oxygen, % 9.7 9.5 9.8 9.667

Carbon Monoxide & Nitrogen, % 79.7 79.74 79.6 79.680

Fuel Factor 1.06 1.06 1.05

Dry Molecular Weight, lb/lb-Mole 30.08 30.10 30.09 30.090

Wet Molecular weight, lb/lb-Mole 29.06 29.05 29.08 29.063

Flue Gas Static Pressure, inches of H2O -2.2 -2.2 -2.2 -2.200

Absolute Flue Gas Pressure, inches of Mercury 29.05 29.02 28.81 28.960

Average Stack Gas Temperature, °F 321.00 318.96 317.58 319.180

Average Velocity Head, inches of H2O 1.9634517155

024

2.058776848

13023

2.107340855

68306

2.043

Average Stack Gas Velocity, feet/second 98.86 101.17 102.58 100.870

Stack Cross-Sectional Area, square feet 113.097 113.097 113.097 113.097

Dry Volumetric Flow Rate, dry scfm 403,133.3 412,032.9 416,944.7 410,703.633

Actual Wet Volumetric Flue Gas Flow Rate, acfm 670,846.2 686,521.4 696,089.4 684,485.667

Percent Isokinetic of Sampling Rate, % 94.0 93.6 92.8 93.467

Percent Excess Air, % 85.5 82.2 87.4 85.033

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

Round Duct Diameter, inches 144 144 144

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

Thursday, February 17, 2011 Page 24 of 29
First Energy, Eastlake Station ICR

9/3/2010

Location Unit 3 Stack - Method 3A CO2

Average

Run Number U3-3ACO2-1 U3-3ACO2-

2

U3-3ACO2-3

Test Date 5/27/2010 5/27/2010 5/27/2010

Run Start Time 8:34:00 AM 11:48:00 AM 3:40:00 PM

Run Finish Time 10:46:00 AM 1:55:00 PM 5:58:00 PM

Carbon Dioxide, % 10 10.2 10 10.067

Oxygen, % 9.3 9.2 9.4 9.300

Fuel Factor 1.16 1.15 1.15

Dry Volumetric Flow Rate, dry scfm 423247 435926 423215 427,462.667

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

Moisture, % 7.3 8.9 8.3 8.167

Analyzer Make California 

Analytical 

Instruments

California 

Analytical 

Instruments

California 

Analytical 

Instruments

Analyzer Model Model 602P Model 602P Model 602P

Analyzer Serial Number

Operating Range 20 20 20 20.000

Operating Units % % %

No. Readings/Avg. 60 60 60 60.000

Calibration Set 0 0 0 0.000

Calibration Pre Zero Cylinder ID EB0012998-

N2

EB0012998-

N2

EB0012998-

N2

Calibration Pre Zero Cylinder Instrument Response 0 0.1 0 0.033

Calibration Pre Zero Cylinder Bias 0 0.5 0 0.167

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID E03NI88E802

318-CO2

E03NI88E80

2318-CO2

E03NI88E80

2318-CO2

Calibration Pre High Cylinder Instrument Response 8.6 8.6 8.6 8.600

Calibration Pre High Cylinder Bias -0.5 -0.5 -0.5 -0.500

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB0012998-

N2

EB0012998-

N2

EB0012998-

N2

Calibration Post Zero Cylinder Instrument Response 0.1 0 0.1 0.067

Calibration Post Zero Cylinder Bias 0.5 0 0.5 0.333

Calibration Post Zero Cylinder Drift 0.5 0.5 0.5 0.500

Calibration Post High Cylinder ID E03NI88E802

318-CO2

E03NI88E80

2318-CO2

E03NI88E80

2318-CO2

Calibration Post High Cylinder Instrument Response 8.6 8.6 8.6 8.600

Calibration Post High Cylinder Bias -0.5 -0.5 -0.5 -0.500

Calibration Post High Cylinder Drift 0 0 0 0.000

Cavg 10 10.2 10 10.067

Cavg Units %vd %vd %vd

Cgas 10.3573 10.5655 10.3573 10.427

Cgas Units %vd %vd %vd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Thursday, February 17, 2011 Page 25 of 29
First Energy, Eastlake Station ICR

9/3/2010

Location Unit 3 Stack - Method 3A O2

Average

Run Number U3-3AO2-1 U3-3AO2-2 U3-3AO2-3

Test Date 5/27/2010 5/27/2010 5/27/2010

Run Start Time 8:34:00 AM 11:48:00 AM 3:40:00 PM

Run Finish Time 10:46:00 AM 1:55:00 PM 5:58:00 PM

Carbon Dioxide, % 10 10.2 10 10.067

Oxygen, % 9.3 9.2 9.4 9.300

Fuel Factor 1.16 1.15 1.15

Dry Volumetric Flow Rate, dry scfm 423247 435926 423215 427,462.667

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

Moisture, % 7.3 8.9 8.3 8.167

Analyzer Make California 

Analytical 

Instruments

California 

Analytical 

Instruments

California 

Analytical 

Instruments

Analyzer Model Model 602P Model 602P Model 602P

Analyzer Serial Number

Operating Range 25 25 25 25.000

Operating Units % % %

No. Readings/Avg. 60 60 60 60.000

Calibration Set 1 1 1 1.000

Calibration Pre Zero Cylinder ID EB0012998-

N2

EB0012998-

N2

EB0012998-

N2

Calibration Pre Zero Cylinder Instrument Response 0.3 0.2 0.2 0.233

Calibration Pre Zero Cylinder Bias 0.8 0.4 0.4 0.533

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC201155-O2 CC201155-

O2

CC201155-

O2

Calibration Pre High Cylinder Instrument Response 12.5 12.4 12.5 12.467

Calibration Pre High Cylinder Bias 0 -0.4 0 -0.133

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB0012998-

N2

EB0012998-

N2

EB0012998-

N2

Calibration Post Zero Cylinder Instrument Response 0.2 0.2 0.2 0.200

Calibration Post Zero Cylinder Bias 0.4 0.4 0.4 0.400

Calibration Post Zero Cylinder Drift 0.4 0 0 0.133

Calibration Post High Cylinder ID CC201155-O2 CC201155-

O2

CC201155-

O2

Calibration Post High Cylinder Instrument Response 12.4 12.5 12.4 12.433

Calibration Post High Cylinder Bias -0.4 0 -0.4 -0.267

Calibration Post High Cylinder Drift 0.4 0.4 0.4 0.400

Cavg 9.3 9.2 9.4 9.300

Cavg Units %vd %vd %vd

Cgas 9.317 9.2278 9.4328 9.326

Cgas Units %vd %vd %vd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Thursday, February 17, 2011 Page 26 of 29
First Energy, Eastlake Station ICR

9/3/2010

Location Unit 3 Stack - Method 6C

Average

Run Number U3-6C-1 U3-6C-2 U3-6C-3

Test Date 5/27/2010 5/27/2010 5/27/2010

Run Start Time 8:34:00 AM 11:48:00 AM 3:40:00 PM

Run Finish Time 10:46:00 AM 1:55:00 PM 5:58:00 PM

Carbon Dioxide, % 10 10.2 10 10.067

Oxygen, % 9.3 9.2 9.4 9.300

Fuel Factor 1.16 1.15 1.15

Dry Volumetric Flow Rate, dry scfm 423247 435926 423215 427,462.667

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

Moisture, % 7.3 8.9 8.3 8.167

Analyzer Make Thermo Thermo Thermo

Analyzer Model Model 43i Model 43i Model 43i

Analyzer Serial Number

Operating Range 1000 1000 1000 1,000.000

Operating Units % ppm ppm

No. Readings/Avg. 60 60 60 60.000

Calibration Set 3 3 3 3.000

Calibration Pre Zero Cylinder ID EB0012998-

N2

EB0012998-

N2

EB0012998-

N2

Calibration Pre Zero Cylinder Instrument Response 4.2 5.3 2 3.833

Calibration Pre Zero Cylinder Bias 0.33 0.44 0.11 0.293

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID ALM008998-

SO2

ALM008998

-SO2

ALM008998-

SO2

Calibration Pre High Cylinder Instrument Response 455.3 468 459 460.767

Calibration Pre High Cylinder Bias -1.67 -0.4 -1.3 -1.123

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB0012998-

N2

EB0012998-

N2

EB0012998-

N2

Calibration Post Zero Cylinder Instrument Response 5.3 2 5.1 4.133

Calibration Post Zero Cylinder Bias 0.44 0.11 0.42 0.323

Calibration Post Zero Cylinder Drift 0.11 0.33 0.31 0.250

Calibration Post High Cylinder ID ALM008998-

SO2

ALM008998

-SO2

ALM008998-

SO2

Calibration Post High Cylinder Instrument Response 468 459 455.4 460.800

Calibration Post High Cylinder Bias -0.4 -1.3 -1.66 -1.120

Calibration Post High Cylinder Drift 1.27 0.9 0.36 0.843

Cavg 679.7 693.2 697 689.967

Cavg Units ppmvd ppmvd ppmvd

Cgas 712.0287 722.7642 736.7858 723.860

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Thursday, February 17, 2011 Page 27 of 29
First Energy, Eastlake Station ICR

9/3/2010

Location Unit 3 Stack - Method 7E

Average

Run Number U3-7E-1 U3-7E-2 U3-7E-3

Test Date 5/27/2010 5/27/2010 5/27/2010

Run Start Time 8:34:00 AM 11:48:00 AM 3:40:00 PM

Run Finish Time 10:46:00 AM 1:55:00 PM 5:58:00 PM

Carbon Dioxide, % 10 10.2 10 10.067

Oxygen, % 9.3 9.2 9.4 9.300

Fuel Factor 1.16 1.15 1.15

Dry Volumetric Flow Rate, dry scfm 423247 435926 423215 427,462.667

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

Moisture, % 7.3 8.9 8.3 8.167

Analyzer Make Teledyne-API TeledyneAPITeledyne-API

Analyzer Model Model 200EH Model 

200EH

Model 200EH

Analyzer Serial Number

Operating Range 200 200 200 200.000

Operating Units ppm ppm ppm

No. Readings/Avg. 60 60 60 60.000

Calibration Set 4 4 4 4.000

Calibration Pre Zero Cylinder ID EB0012998-

N2

EB0012998-

N2

EB0012998-

N2

Calibration Pre Zero Cylinder Instrument Response 1 0.9 1.1 1.000

Calibration Pre Zero Cylinder Bias 0.25 0.2 0.3 0.250

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID ALMX068001

-Nox

ALMX06800

1-Nox

ALMX06800

1-Nox

Calibration Pre High Cylinder Instrument Response 94.7 95.6 93 94.433

Calibration Pre High Cylinder Bias -0.55 -0.1 -1.4 -0.683

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB0012998-

N2

EB0012998-

N2

EB0012998-

N2

Calibration Post Zero Cylinder Instrument Response 0.9 1.1 1.3 1.100

Calibration Post Zero Cylinder Bias 0.2 0.3 0.4 0.300

Calibration Post Zero Cylinder Drift 0.05 0.1 0.1 0.083

Calibration Post High Cylinder ID ALMX068001

-Nox

ALMX06800

1-Nox

ALMX06800

1-Nox

Calibration Post High Cylinder Instrument Response 95.6 93 90.2 92.933

Calibration Post High Cylinder Bias -0.1 -1.4 -2.8 -1.433

Calibration Post High Cylinder Drift 0.45 1.3 1.4 1.050

Cavg 114.2 122.2 118.1 118.167

Cavg Units ppmvd ppmvd ppmvd

Cgas 114.6927 123.928 123.3657 120.662

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Thursday, February 17, 2011 Page 28 of 29
First Energy, Eastlake Station ICR

9/3/2010

Location Unit 3 Stack - OTM - 27/28

Average

Run Number 1 2 3

Test Date 5/25/2010 5/26/2010 5/26/2010

Run Start Time

Run Finish Time

Net Traversing Points 12 12 12

Net Run Time, minutes 343.25 371.5 375.5

Nozzle Diameter, inches 0.131 0.131 0.131 0.131

Pitot Tube Coefficient 0.826 0.826 0.826 0.826

Dry Gas Meter Calibration Factor 1.047 1.047 1.047 1.047

Barometric Pressure, inches of Mercury 29.21 29.1 28.94 29.083

Average Orifice Meter Differential, inches H2O 0.48 0.48 0.48 0.480

Dry Gas Meter Volume Sampled, cubic feet 135.346 146.841 149.535 143.907

Average Dry Gas Meter Temperature, °F 120.38 120.29 122.67 121.113

Dry Gas Meter Volume Sampled, dscf 126.011 136.220 137.394 133.208

Total Moisture Liquid collected, g 185.3 248.2 261.4 231.633

Volume of Water Vapor, standard cubic feet 8.72 11.68 12.30 10.900

Moisture Content of Stack Gas, % 6.47 7.90 8.22 7.530

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

Dry Mole Fraction 0.9353 0.921 0.9178 0.925

Carbon Dioxide, % 10.5 10.5 10.5 10.500

Oxygen, % 9 9 9 9.000

Carbon Monoxide & Nitrogen, % 80.5 80.5 80.5 80.500

Fuel Factor 1.13 1.13 1.13

Dry Molecular Weight, lb/lb-Mole 30.04 30.04 30.04 30.040

Wet Molecular weight, lb/lb-Mole 29.26 29.09 29.05 29.133

Flue Gas Static Pressure, inches of H2O -2.19 -2.19 -2.19 -2.190

Absolute Flue Gas Pressure, inches of Mercury 29.05 28.94 28.78 28.923

Average Stack Gas Temperature, °F 312.33 311.25 317.42 313.667

Average Velocity Head, inches of H2O 2.0777217054

5151

2.212775702

10396

2.261812325

93758

2.184

Average Stack Gas Velocity, feet/second 97.02 100.54 102.41 99.990

Stack Cross-Sectional Area, square feet 113.097 113.097 113.097 113.097

Dry Volumetric Flow Rate, dry scfm 408,724.0 416,079.7 416,677.6 413,827.100

Actual Wet Volumetric Flue Gas Flow Rate, acfm 658,360.3 682,246.3 694,935.8 678,514.133

Percent Isokinetic of Sampling Rate, % 108.5 106.5 106.1 107.033

Percent Excess Air, % 73.5 73.5 73.5 73.500

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

Round Duct Diameter, inches 144 144 144

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

Thursday, February 17, 2011 Page 29 of 29