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 1

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. Units 1 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 1 Stack 144 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 1 Stack - Method 0011

Average

Run Number U1-M0011-1 U1-M0011-

2

U1-M0011-3

Test Date 5/19/2010 5/19/2010 5/20/2010

Run Start Time 1:18:00 PM 4:24:00 PM 8:03:00 AM

Run Finish Time 3:08:00 PM 6:14:00 PM 9:53:00 AM

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 72.739 70.049 68.250 70.346

Moisture Content of Stack Gas, % 9.76 9.73 9.15 9.547

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

Carbon Dioxide, % 10.9 10.6 10.7 10.733

Oxygen, % 9.4 9.7 9.6 9.567

Average Stack Gas Temperature, °F 329.50 328.67 324.83 327.667

Dry Volumetric Flow Rate, dry scfm 362,780.2 365,633.9 358,666.2 362,360.100

Actual Wet Volumetric Flue Gas Flow Rate, acfm 624,499.0 628,977.7 607,534.5 620,337.067

Percent Isokinetic of Sampling Rate, % 98.0 93.7 93.0 94.900

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 1 Stack - Method 10

Average

Run Number U1-M10-1 U1-M10-2 U1-M10-3

Test Date 5/24/2010 5/24/2010 5/24/2010

Run Start Time 1:47:00 PM 4:31:00 PM 7:10:00 PM

Run Finish Time 3:58:00 PM 6:38:00 PM 9:20:00 PM

Carbon Dioxide, % 10.5 10.5 10.6 10.533

Oxygen, % 8.6 8.5 8.5 8.533

Dry Volumetric Flow Rate, dry scfm 436139 433325 438472 435,978.667

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

Moisture, % 9.1 9.2 9.1 9.133

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 1 Stack - Method 25A

Average

Run Number U1-25A-1 U1-25A-2 U1-25A-3

Test Date 5/24/2010 5/24/2010 5/24/2010

Run Start Time 1:47:00 PM 4:31:00 PM 7:10:00 PM

Run Finish Time 3:58:00 PM 6:38:00 PM 9:20:00 PM

Carbon Dioxide, % 10.5 10.5 10.6 10.533

Oxygen, % 8.6 8.5 8.5 8.533

Dry Volumetric Flow Rate, dry scfm 436139 433325 438472 435,978.667

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

Moisture, % 9.1 9.2 9.1 9.133

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Unit 1 Stack - Method 26A

Average

Run Number U1-26A-1 U1-26A-2 U1-26A-3

Test Date 5/24/2010 5/24/2010 5/24/2010

Run Start Time 1:57:00 PM 4:40:00 PM 4:40:00 PM

Run Finish Time 2:52:00 PM 5:35:00 PM 5:35:00 PM

Net Run Time, minutes 60 60 60

Dry Gas Meter Volume Sampled, dscf 38.212 37.910 38.282 38.135

Moisture Content of Stack Gas, % 9.13 9.20 9.09 9.140

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

Carbon Dioxide, % 11.4 11.1 11.8 11.433

Oxygen, % 8.9 9.2 8.5 8.867

Average Stack Gas Temperature, °F 332.42 332.67 332.25 332.447

Dry Volumetric Flow Rate, dry scfm 381,686.7 378,888.3 383,697.3 381,424.100

Actual Wet Volumetric Flue Gas Flow Rate, acfm 649,267.3 645,874.3 653,610.2 649,583.933

Percent Isokinetic of Sampling Rate, % 97.9 97.8 97.6 97.767

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 1 Stack - Method 29

Average

Run Number U1-M29-1 U1-M29-2 U1-M29-3

Test Date 5/18/2010 5/19/2010 5/19/2010

Run Start Time 10:35:00 AM 8:13:00 

AM

1:32:00 PM

Run Finish Time 2:25:00 PM 12:03:00 

PM

5:22:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 151.228 150.265 150.259 150.584

Moisture Content of Stack Gas, % 9.89 9.76 10.16 9.937

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

Carbon Dioxide, % 10.7 10.76 10.9 10.787

Oxygen, % 9.6 9.55 9.4 9.517

Average Stack Gas Temperature, °F 332.67 332.79 334.04 333.167

Dry Volumetric Flow Rate, dry scfm 373,931.4 371,038.6 370,122.3 371,697.433

Actual Wet Volumetric Flue Gas Flow Rate, acfm 645,195.8 638,274.2 643,431.5 642,300.500

Percent Isokinetic of Sampling Rate, % 96.8 96.9 97.2 96.967

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 1 Stack - Method 3A CO2

Average

Run Number U1-3ACO2-

1

U1-

3ACO2-2

U1-3ACO2-

3

Test Date 5/24/2010 5/24/2010 5/24/2010

Run Start Time 1:47:00 PM 4:31:00 PM 7:10:00 PM

Run Finish Time 3:58:00 PM 6:38:00 PM 9:20:00 PM

Carbon Dioxide, % 10.5 10.5 10.6 10.533

Oxygen, % 8.6 8.5 8.5 8.533

Dry Volumetric Flow Rate, dry scfm 436139 433325 438472 435,978.667

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

Moisture, % 9.1 9.2 9.1 9.133

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 1 Stack - Method 3A O2

Average

Run Number U1-3AO2-1 U1-3AO2-

2

U1-3AO2-3

Test Date 5/24/2010 5/24/2010 5/24/2010

Run Start Time 1:47:00 PM 4:31:00 PM 7:10:00 PM

Run Finish Time 3:58:00 PM 6:38:00 PM 9:20:00 PM

Carbon Dioxide, % 10.5 10.5 10.6 10.533

Oxygen, % 8.6 8.5 8.5 8.533

Dry Volumetric Flow Rate, dry scfm 436139 433325 438472 435,978.667

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

Moisture, % 9.1 9.2 9.1 9.133

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Unit 1 Stack - Method 6C

Average

Run Number U1-6C-1 U1-6C-2 U1-6C-3

Test Date 5/24/2010 5/24/2010 5/24/2010

Run Start Time 1:47:00 PM 4:31:00 PM 7:10:00 PM

Run Finish Time 3:58:00 PM 6:38:00 PM 9:20:00 PM

Carbon Dioxide, % 10.5 10.5 10.6 10.533

Oxygen, % 8.6 8.5 8.5 8.533

Dry Volumetric Flow Rate, dry scfm 436139 433325 438472 435,978.667

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

Moisture, % 9.1 9.2 9.1 9.133

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 1 Stack - Method 7E

Average

Run Number U1-7E-1 U1-7E-2 U1-7E-3

Test Date 5/24/2010 5/24/2010 5/24/2010

Run Start Time 1:47:00 PM 4:31:00 PM 7:10:00 PM

Run Finish Time 3:58:00 PM 6:38:00 PM 9:20:00 PM

Carbon Dioxide, % 10.5 10.5 10.6 10.533

Oxygen, % 8.6 8.5 8.5 8.533

Dry Volumetric Flow Rate, dry scfm 436139 436139 438472 436,916.667

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

Moisture, % 9.1 9.2 9.1 9.133

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Unit 1 Stack - OTM - 27/28

Average

Run Number U1-

OTM27/28-1

U1-

OTM27/28

-2

U1-

OTM27/28-3

Test Date 5/18/2010 5/19/2010 5/20/2010

Run Start Time

Run Finish Time

Net Run Time, minutes 288 362.5 359.75

Dry Gas Meter Volume Sampled, dscf 105.230 131.690 131.435 122.785

Moisture Content of Stack Gas, % 9.96 9.34 8.90 9.400

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

Carbon Dioxide, % 10.7 10.7 10.7 10.700

Oxygen, % 9.6 9.6 9.6 9.600

Average Stack Gas Temperature, °F 325.42 328.25 327.42 327.030

Dry Volumetric Flow Rate, dry scfm 350,718.2 368,892.3 371,055.5 363,555.333

Actual Wet Volumetric Flue Gas Flow Rate, acfm 599,866.5 626,941.9 623,684.7 616,831.033

Percent Isokinetic of Sampling Rate, % 97.3 92.0 92.0 93.767

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 1 Stack - Method 0011

Compound: Formaldehyde

Average

RunNumber U1-M0011-1 U1-M0011-2 U1-M0011-3

Mass_mg 0.01 0.032 0.022 0.021

Elb/hr 6.60E-03 2.21E-02 1.53E-02 0.015

gr/dscf 2.12E-06 7.05E-06 4.97E-06 0.000

lb/mmBtuO2 5.39E-06 1.84E-05 1.29E-05 0.000

mg/dscm 4.86E-03 1.61E-02 1.14E-02 0.011

ppm 3.89E-03 1.29E-02 9.12E-03 0.009

Location: Unit 1 Stack - Method 10

Compound: Carbon Monoxide

Average

Run U1-M10-1 U1-M10-2 U1-M10-3

Elb/hr 7.12E+01 6.62E+01 9.02E+01 75.867

lb/mmBtuO2 4.52E-02 4.20E-02 5.65E-02 0.048

ppm 3.74E+01 3.50E+01 4.72E+01 39.867

Location: Unit 1 Stack - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run U1-25A-1 U1-25A-2 U1-25A-3

Elb/hr 9.70E-01 1.14E+00 9.84E-01 1.031

lb/mmBtuO2 6.16E-04 7.20E-04 6.17E-04 0.001

ppm 3.24E-01 3.82E-01 3.27E-01 0.344

Location: Unit 1 Stack - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber U1-26A-1 U1-26A-2 U1-26A-3

Mass_mg 54.4486 52.3776 40.5292 49.118

Elb/hr 7.19E+01 6.92E+01 5.37E+01 64.933

lb/mmBtuO2 5.35E-02 5.32E-02 3.85E-02 0.048

mg/dscm 5.03E+01 4.88E+01 3.74E+01 45.500

ppm 3.32E+01 3.22E+01 2.47E+01 30.033

Compound: Hydrogen Fluoride

Average

RunNumber U1-26A-1 U1-26A-2 U1-26A-3

Mass_mg 3.8708 3.9719 4.2203 4.021

Elb/hr 5.11E+00 5.25E+00 5.60E+00 5.320

lb/mmBtuO2 3.80E-03 4.04E-03 4.01E-03 0.004

mg/dscm 3.58E+00 3.70E+00 3.89E+00 3.723

ppm 4.30E+00 4.45E+00 4.68E+00 4.477

Location: Unit 1 Stack - Method 29

Compound: Antimony

Average

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

9/3/2010

RunNumber U1-M29-1 U1-M29-2 U1-M29-3

Mass_mg 0.0398445 0.0002798 0.0001613 0.013

Elb/hr 1.30E-02 9.14E-05 5.26E-05 0.004

gr/dscf 4.07E-06 2.87E-08 1.66E-08 0.000

lb/mmBtuO2 1.05E-05 7.39E-08 4.21E-08 0.000

mg/dscm 9.31E-03 6.58E-05 3.79E-05 0.003

ppm 1.84E-03 1.30E-05 7.49E-06 0.001

Compound: Arsenic

Average

RunNumber U1-M29-1 U1-M29-2 U1-M29-3

Mass_mg 0.0008837 0.0008693 0.0009085 0.001

Elb/hr 2.89E-04 2.84E-04 2.96E-04 0.000

gr/dscf 9.02E-08 8.93E-08 9.33E-08 0.000

lb/mmBtuO2 2.33E-07 2.30E-07 2.37E-07 0.000

mg/dscm 2.06E-04 2.04E-04 2.14E-04 0.000

ppm 6.63E-05 6.56E-05 6.86E-05 0.000

Compound: Beryllium

Average

RunNumber U1-M29-1 U1-M29-2 U1-M29-3

Mass_mg 0.00005375 0.000067 0.0000663 0.000

Elb/hr 1.76E-05 2.19E-05 2.16E-05 0.000

gr/dscf 5.49E-09 6.88E-09 6.81E-09 0.000

lb/mmBtuO2 1.42E-08 1.77E-08 1.73E-08 0.000

mg/dscm 1.26E-05 1.57E-05 1.56E-05 0.000

ppm 3.35E-05 4.20E-05 4.16E-05 0.000

Compound: Cadmium

Average

RunNumber U1-M29-1 U1-M29-2 U1-M29-3

Mass_mg 0.0000723 0.000087 0.000034 0.000

Elb/hr 2.36E-05 2.84E-05 1.11E-05 0.000

gr/dscf 7.38E-09 8.93E-09 3.49E-09 0.000

lb/mmBtuO2 1.91E-08 2.30E-08 8.87E-09 0.000

mg/dscm 1.69E-05 2.04E-05 7.99E-06 0.000

ppm 3.61E-06 4.38E-06 1.71E-06 0.000

Compound: Chromium

Average

RunNumber U1-M29-1 U1-M29-2 U1-M29-3

Mass_mg 0.014952 0.00686 0.007947 0.010

Elb/hr 4.89E-03 2.24E-03 2.59E-03 0.003

gr/dscf 1.53E-06 7.05E-07 8.16E-07 0.000

lb/mmBtuO2 3.94E-06 1.81E-06 2.07E-06 0.000

mg/dscm 3.49E-03 1.61E-03 1.87E-03 0.002

ppm 1.62E-03 7.46E-04 8.64E-04 0.001

Compound: Cobalt

Average

RunNumber U1-M29-1 U1-M29-2 U1-M29-3

Mass_mg 0.0013482 0.013684 0.0010066 0.005

Elb/hr 4.41E-04 4.47E-03 3.28E-04 0.002

gr/dscf 1.38E-07 1.41E-06 1.03E-07 0.000

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

9/3/2010

Process Run Data

lb/mmBtuO2 3.56E-07 3.62E-06 2.63E-07 0.000

mg/dscm 3.15E-04 3.22E-03 2.37E-04 0.001

ppm 1.29E-04 1.31E-03 9.66E-05 0.001

Compound: Filterable Particulate

Average

RunNumber U1-M29-1 U1-M29-2 U1-M29-3

Mass_mg 21.2 20.35 23.2 21.583

Elb/hr 6.93E+00 6.65E+00 7.56E+00 7.047

gr/dscf 2.16E-03 2.09E-03 2.38E-03 0.002

lb/mmBtuO2 5.59E-03 5.38E-03 6.05E-03 0.006

mg/dscm 4.95E+00 4.78E+00 5.45E+00 5.060

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 1 Stack - Method 0011

Average

Run Number U1-M0011-1 U1-M0011-2 U1-M0011-3

Test Date 5/19/2010 5/19/2010 5/20/2010

Run Start Time 1:18:00 PM 4:24:00 PM 8:03:00 AM

Run Finish Time 3:08:00 PM 6:14:00 PM 9:53:00 AM

Net Traversing Points 13 13 13

Net Run Time, minutes 120 120 120

Nozzle Diameter, inches 0.188 0.188 0.188 0.188

Pitot Tube Coefficient 0.858 0.858 0.858 0.858

Dry Gas Meter Calibration Factor 0.955 0.955 0.955 0.955

Barometric Pressure, inches of Mercury 28.97 28.97 29.06 29.000

Average Orifice Meter Differential, inches H2O 1.49 1.45 1.37 1.437

Dry Gas Meter Volume Sampled, cubic feet 83.105 80.999 78.962 81.022

Average Dry Gas Meter Temperature, °F 99.92 106.63 108.58 105.043

Dry Gas Meter Volume Sampled, dscf 72.739 70.049 68.250 70.346

Total Moisture Liquid collected, g 167.3 160.5 145.9 157.900

Volume of Water Vapor, standard cubic feet 7.87 7.55 6.87 7.430

Moisture Content of Stack Gas, % 9.76 9.73 9.15 9.547

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

Dry Mole Fraction 0.9024 0.9027 0.9085 0.905

Carbon Dioxide, % 10.9 10.6 10.7 10.733

Oxygen, % 9.4 9.7 9.6 9.567

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 30.12 30.08 30.10 30.100

Wet Molecular weight, lb/lb-Mole 28.94 28.90 28.99 28.943

Flue Gas Static Pressure, inches of H2O -2.33 -2.58 -2.2 -2.370

Absolute Flue Gas Pressure, inches of Mercury 28.80 28.78 28.90 28.827

Average Stack Gas Temperature, °F 329.50 328.67 324.83 327.667

Average Velocity Head, inches of H2O 1.6619272548

3942

1.684075508

43856

1.590348899

87894

1.645

Average Stack Gas Velocity, feet/second 92.03 92.69 89.53 91.417

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

Dry Volumetric Flow Rate, dry scfm 362,780.2 365,633.9 358,666.2 362,360.100

Actual Wet Volumetric Flue Gas Flow Rate, acfm 624,499.0 628,977.7 607,534.5 620,337.067

Percent Isokinetic of Sampling Rate, % 98.0 93.7 93.0 94.900

Percent Excess Air, % 80.8 85.5 83.9 83.400

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 1 Stack - Method 10

Average

Run Number U1-M10-1 U1-M10-2 U1-M10-3

Test Date 5/24/2010 5/24/2010 5/24/2010

Run Start Time 1:47:00 PM 4:31:00 PM 7:10:00 PM

Run Finish Time 3:58:00 PM 6:38:00 PM 9:20:00 PM

Carbon Dioxide, % 10.5 10.5 10.6 10.533

Oxygen, % 8.6 8.5 8.5 8.533

Fuel Factor 1.17 1.18 1.17

Dry Volumetric Flow Rate, dry scfm 436139 433325 438472 435,978.667

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

Moisture, % 9.1 9.2 9.1 9.133

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 2.9 0.2 -1 0.700

Calibration Pre Zero Cylinder Bias 2.7 0 -1.2 0.500

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID XL001279BCOXL001279BCOXL001279BCO

Calibration Pre High Cylinder Instrument Response 34.7 29.8 29.3 31.267

Calibration Pre High Cylinder Bias 4.1 -0.8 -1.3 0.667

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 -0.3 -1 0.6 -0.233

Calibration Post Zero Cylinder Bias -0.5 -1.2 0.4 -0.433

Calibration Post Zero Cylinder Drift 3.2 1.2 1.6 2.000

Calibration Post High Cylinder ID XL001279BCOXL001279BCOXL001279BCO

Calibration Post High Cylinder Instrument Response 29.8 29.3 32.3 30.467

Calibration Post High Cylinder Bias -0.8 -1.3 1.7 -0.133

Calibration Post High Cylinder Drift 4.9 0.5 3 2.800

Cavg 39.1 33.8 47.5 40.133

Cavg Units ppmvd ppmvd ppmvd

Cgas 37.4458 35.0108 47.1768 39.878

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 1 Stack - Method 25A

Average

Run Number U1-25A-1 U1-25A-2 U1-25A-3

Test Date 5/24/2010 5/24/2010 5/24/2010

Run Start Time 1:47:00 PM 4:31:00 PM 7:10:00 PM

Run Finish Time 3:58:00 PM 6:38:00 PM 9:20:00 PM

Carbon Dioxide, % 10.5 10.5 10.6 10.533

Oxygen, % 8.6 8.5 8.5 8.533

Fuel Factor 1.17 1.18 1.17

Dry Volumetric Flow Rate, dry scfm 436139 433325 438472 435,978.667

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

Moisture, % 9.1 9.2 9.1 9.133

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 -0.1 -0.1 -0.2 -0.133

Calibration Pre Zero Cylinder Bias -1 -1 -2 -1.333

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 5.3 5.1 5.1 5.167

Calibration Pre High Cylinder Bias 1 -1 -1 -0.333

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 -0.1 -0.2 -0.2 -0.167

Calibration Post Zero Cylinder Bias -1 -2 -2 -1.667

Calibration Post Zero Cylinder Drift 0 1 0 0.333

Calibration Post High Cylinder ID ALM027314-

VOC

ALM027314

-VOC

ALM027314-

VOC

Calibration Post High Cylinder Instrument Response 5.1 5.1 5 5.067

Calibration Post High Cylinder Bias -1 -1 -2 -1.333

Calibration Post High Cylinder Drift 2 0 1 1.000

Cavg 0.2 0.2 0.1 0.167

Cavg Units ppmvw ppmvw ppmvw

Cgas 0.3238 0.3818 0.3269 0.344

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 0.2943396226

4151

0.346666666

666667

0.297142857

142857

0.313

Cgasw Units ppmvw ppmvw ppmvw

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

9/3/2010

Location Unit 1 Stack - Method 26A

Average

Run Number U1-26A-1 U1-26A-2 U1-26A-3

Test Date 5/24/2010 5/24/2010 5/24/2010

Run Start Time 1:57:00 PM 4:40:00 PM 4:40:00 PM

Run Finish Time 2:52:00 PM 5:35:00 PM 5:35:00 PM

Net Traversing Points 13 13 13

Net Run Time, minutes 60 60 60

Nozzle Diameter, inches 0.188 0.188 0.188 0.188

Pitot Tube Coefficient 0.826 0.826 0.826 0.826

Dry Gas Meter Calibration Factor 0.955 0.955 0.955 0.955

Barometric Pressure, inches of Mercury 29.21 29.18 29.15 29.180

Average Orifice Meter Differential, inches H2O 1.69 1.67 1.71 1.690

Dry Gas Meter Volume Sampled, cubic feet 43.800 44.400 44.800 44.333

Average Dry Gas Meter Temperature, °F 106.67 118.38 117.38 114.143

Dry Gas Meter Volume Sampled, dscf 38.212 37.910 38.282 38.135

Total Moisture Liquid collected, g 81.6 81.6 81.4 81.533

Volume of Water Vapor, standard cubic feet 3.84 3.84 3.83 3.837

Moisture Content of Stack Gas, % 9.13 9.20 9.09 9.140

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

Dry Mole Fraction 0.9087 0.908 0.9091 0.909

Carbon Dioxide, % 11.4 11.1 11.8 11.433

Oxygen, % 8.9 9.2 8.5 8.867

Carbon Monoxide & Nitrogen, % 79.7 79.7 79.7 79.700

Fuel Factor 1.05 1.05 1.05

Dry Molecular Weight, lb/lb-Mole 30.18 30.14 30.23 30.183

Wet Molecular weight, lb/lb-Mole 29.07 29.02 29.12 29.070

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

Absolute Flue Gas Pressure, inches of Mercury 29.05 29.02 28.99 29.020

Average Stack Gas Temperature, °F 332.42 332.67 332.25 332.447

Average Velocity Head, inches of H2O 1.9563441691

6607

1.930045016

63504

1.982641374

84142

1.956

Average Stack Gas Velocity, feet/second 95.68 95.18 96.32 95.727

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

Dry Volumetric Flow Rate, dry scfm 381,686.7 378,888.3 383,697.3 381,424.100

Actual Wet Volumetric Flue Gas Flow Rate, acfm 649,267.3 645,874.3 653,610.2 649,583.933

Percent Isokinetic of Sampling Rate, % 97.9 97.8 97.6 97.767

Percent Excess Air, % 73.3 77.7 67.8 72.933

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 1 Stack - Method 29

Average

Run Number U1-M29-1 U1-M29-2 U1-M29-3

Test Date 5/18/2010 5/19/2010 5/19/2010

Run Start Time 10:35:00 AM 8:13:00 AM 1:32:00 PM

Run Finish Time 2:25:00 PM 12:03:00 PM 5:22:00 PM

Net Traversing Points 25 25 25

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.19 0.19 0.19 0.190

Pitot Tube Coefficient 0.863 0.863 0.863 0.863

Dry Gas Meter Calibration Factor 0.958 0.958 0.958 0.958

Barometric Pressure, inches of Mercury 29.05 29.1 28.97 29.040

Average Orifice Meter Differential, inches H2O 1.57 1.54 1.56 1.557

Dry Gas Meter Volume Sampled, cubic feet 173.220 171.860 172.600 172.560

Average Dry Gas Meter Temperature, °F 104.77 104.85 104.81 104.810

Dry Gas Meter Volume Sampled, dscf 151.228 150.265 150.259 150.584

Total Moisture Liquid collected, g 352.6 345.3 361.2 353.033

Volume of Water Vapor, standard cubic feet 16.60 16.25 17.00 16.617

Moisture Content of Stack Gas, % 9.89 9.76 10.16 9.937

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

Dry Mole Fraction 0.9011 0.9024 0.8984 0.901

Carbon Dioxide, % 10.7 10.76 10.9 10.787

Oxygen, % 9.6 9.55 9.4 9.517

Carbon Monoxide & Nitrogen, % 79.7 79.69 79.7 79.697

Fuel Factor 1.06 1.05 1.06

Dry Molecular Weight, lb/lb-Mole 30.10 30.10 30.12 30.107

Wet Molecular weight, lb/lb-Mole 28.90 28.92 28.89 28.903

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

Absolute Flue Gas Pressure, inches of Mercury 28.89 28.94 28.81 28.880

Average Stack Gas Temperature, °F 332.67 332.79 334.04 333.167

Average Velocity Head, inches of H2O 1.7495118597

0597

1.715855497

83247

1.731541995

53635

1.732

Average Stack Gas Velocity, feet/second 95.08 94.06 94.82 94.653

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

Dry Volumetric Flow Rate, dry scfm 373,931.4 371,038.6 370,122.3 371,697.433

Actual Wet Volumetric Flue Gas Flow Rate, acfm 645,195.8 638,274.2 643,431.5 642,300.500

Percent Isokinetic of Sampling Rate, % 96.8 96.9 97.2 96.967

Percent Excess Air, % 83.9 83.1 80.8 82.600

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 1 Stack - Method 3A CO2

Average

Run Number U1-3ACO2-1 U1-3ACO2-

2

U1-3ACO2-3

Test Date 5/24/2010 5/24/2010 5/24/2010

Run Start Time 1:47:00 PM 4:31:00 PM 7:10:00 PM

Run Finish Time 3:58:00 PM 6:38:00 PM 9:20:00 PM

Carbon Dioxide, % 10.5 10.5 10.6 10.533

Oxygen, % 8.6 8.5 8.5 8.533

Fuel Factor 1.17 1.18 1.17

Dry Volumetric Flow Rate, dry scfm 436139 433325 438472 435,978.667

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

Moisture, % 9.1 9.2 9.1 9.133

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 0.1 0 0 0.033

Calibration Pre Zero Cylinder Bias 0.5 0 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 8.4 8.5 8.4 8.433

Calibration Pre High Cylinder Bias -1.5 -1 -1.5 -1.333

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 0 0 0.000

Calibration Post Zero Cylinder Bias 0 0 0 0.000

Calibration Post Zero Cylinder Drift 0.5 0 0 0.167

Calibration Post High Cylinder ID E03NI88E802

318-CO2

E03NI88E80

2318-CO2

E03NI88E80

2318-CO2

Calibration Post High Cylinder Instrument Response 8.5 8.4 8.4 8.433

Calibration Post High Cylinder Bias -1 -1.5 -1.5 -1.333

Calibration Post High Cylinder Drift 0.5 0.5 0 0.333

Cavg 10.5 10.5 10.6 10.533

Cavg Units %vd %vd %vd

Cgas 11.072 11.0592 11.231 11.121

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 1 Stack - Method 3A O2

Average

Run Number U1-3AO2-1 U1-3AO2-2 U1-3AO2-3

Test Date 5/24/2010 5/24/2010 5/24/2010

Run Start Time 1:47:00 PM 4:31:00 PM 7:10:00 PM

Run Finish Time 3:58:00 PM 6:38:00 PM 9:20:00 PM

Carbon Dioxide, % 10.5 10.5 10.6 10.533

Oxygen, % 8.6 8.5 8.5 8.533

Fuel Factor 1.17 1.18 1.17

Dry Volumetric Flow Rate, dry scfm 436139 433325 438472 435,978.667

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

Moisture, % 9.1 9.2 9.1 9.133

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 12.4 12.4 12.3 12.367

Calibration Pre High Cylinder Bias -0.4 -0.4 -0.8 -0.533

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 0.3 0.233

Calibration Post Zero Cylinder Bias 0.4 0.4 0.8 0.533

Calibration Post Zero Cylinder Drift 0.4 0 0.4 0.267

Calibration Post High Cylinder ID CC201155-O2 CC201155-

O2

CC201155-

O2

Calibration Post High Cylinder Instrument Response 12.4 12.3 12.4 12.367

Calibration Post High Cylinder Bias -0.4 -0.8 -0.4 -0.533

Calibration Post High Cylinder Drift 0 0.8 0.4 0.400

Cavg 8.6 8.5 8.5 8.533

Cavg Units %vd %vd %vd

Cgas 8.6318 8.5801 8.5636 8.592

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 1 Stack - Method 6C

Average

Run Number U1-6C-1 U1-6C-2 U1-6C-3

Test Date 5/24/2010 5/24/2010 5/24/2010

Run Start Time 1:47:00 PM 4:31:00 PM 7:10:00 PM

Run Finish Time 3:58:00 PM 6:38:00 PM 9:20:00 PM

Carbon Dioxide, % 10.5 10.5 10.6 10.533

Oxygen, % 8.6 8.5 8.5 8.533

Fuel Factor 1.17 1.18 1.17

Dry Volumetric Flow Rate, dry scfm 436139 433325 438472 435,978.667

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

Moisture, % 9.1 9.2 9.1 9.133

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 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 6.5 6.2 5.9 6.200

Calibration Pre Zero Cylinder Bias 0.56 0.53 0.5 0.530

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 458.6 467.2 461 462.267

Calibration Pre High Cylinder Bias -1.34 -0.48 -1.1 -0.973

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 6.2 5.9 5 5.700

Calibration Post Zero Cylinder Bias 0.53 0.5 0.41 0.480

Calibration Post Zero Cylinder Drift 0.03 0.03 0.09 0.050

Calibration Post High Cylinder ID ALM008998-

SO2

ALM008998

-SO2

ALM008998-

SO2

Calibration Post High Cylinder Instrument Response 467.2 461 460.1 462.767

Calibration Post High Cylinder Bias -0.48 -1.1 -1.19 -0.923

Calibration Post High Cylinder Drift 0.86 0.62 8.999999999

99999E-02

0.523

Cavg 696.5 706.7 540.1 647.767

Cavg Units ppmvd ppmvd ppmvd

Cgas 728.6218 737.2848 566.252 677.386

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 1 Stack - Method 7E

Average

Run Number U1-7E-1 U1-7E-2 U1-7E-3

Test Date 5/24/2010 5/24/2010 5/24/2010

Run Start Time 1:47:00 PM 4:31:00 PM 7:10:00 PM

Run Finish Time 3:58:00 PM 6:38:00 PM 9:20:00 PM

Carbon Dioxide, % 10.5 10.5 10.6 10.533

Oxygen, % 8.6 8.5 8.5 8.533

Fuel Factor 1.17 1.18 1.17

Dry Volumetric Flow Rate, dry scfm 436139 436139 438472 436,916.667

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

Moisture, % 9.1 9.2 9.1 9.133

Analyzer Make Teledyne/API 

Instruments

Teledyne/AP

I Instruments

Teledyne/API

 Instruments

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 0.5 1.2 0.8 0.833

Calibration Pre Zero Cylinder Bias 0 0.35 0.15 0.167

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 92.1 91.4 90.2 91.233

Calibration Pre High Cylinder Bias -1.85 -2.2 -2.8 -2.283

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 1.2 0.8 1 1.000

Calibration Post Zero Cylinder Bias 0.35 0.15 0.25 0.250

Calibration Post Zero Cylinder Drift 0.35 0.2 0.1 0.217

Calibration Post High Cylinder ID ALMX068001

-Nox

ALMX06800

1-Nox

ALMX06800

1-Nox

Calibration Post High Cylinder Instrument Response 91.4 90.2 90.9 90.833

Calibration Post High Cylinder Bias -2.2 -2.8 -2.45 -2.483

Calibration Post High Cylinder Drift 0.35 0.6 0.35 0.433

Cavg 142.9 136.5 123.8 134.400

Cavg Units ppmvd ppmvd ppmvd

Cgas 149.0822 143.9499 130.7826 141.272

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 1 Stack - OTM - 27/28

Average

Run Number U1-

OTM27/28-1

U1-

OTM27/28-2

U1-

OTM27/28-3

Test Date 5/18/2010 5/19/2010 5/20/2010

Run Start Time

Run Finish Time

Net Traversing Points 12 12 12

Net Run Time, minutes 288 362.5 359.75

Nozzle Diameter, inches 0.149 0.149 0.149 0.149

Pitot Tube Coefficient 0.826 0.858 0.858 0.847

Dry Gas Meter Calibration Factor 1.047 1.047 1.047 1.047

Barometric Pressure, inches of Mercury 29.05 29.14 29.29 29.160

Average Orifice Meter Differential, inches H2O 0.49 0.48 0.48 0.483

Dry Gas Meter Volume Sampled, cubic feet 110.404 137.520 138.288 128.737

Average Dry Gas Meter Temperature, °F 103.83 102.92 110.08 105.610

Dry Gas Meter Volume Sampled, dscf 105.230 131.690 131.435 122.785

Total Moisture Liquid collected, g 247.2 288.2 272.8 269.400

Volume of Water Vapor, standard cubic feet 11.64 13.57 12.84 12.683

Moisture Content of Stack Gas, % 9.96 9.34 8.90 9.400

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

Dry Mole Fraction 0.9004 0.9066 0.911 0.906

Carbon Dioxide, % 10.7 10.7 10.7 10.700

Oxygen, % 9.6 9.6 9.6 9.600

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 30.10 30.10 30.10 30.100

Wet Molecular weight, lb/lb-Mole 28.89 28.97 29.02 28.960

Flue Gas Static Pressure, inches of H2O -2.05 -2.05 -2.05 -2.050

Absolute Flue Gas Pressure, inches of Mercury 28.90 28.99 29.14 29.010

Average Stack Gas Temperature, °F 325.42 328.25 327.42 327.030

Average Velocity Head, inches of H2O 1.6660116450

304

1.690221815

42986

1.686272374

02982

1.681

Average Stack Gas Velocity, feet/second 88.40 92.39 91.91 90.900

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

Dry Volumetric Flow Rate, dry scfm 350,718.2 368,892.3 371,055.5 363,555.333

Actual Wet Volumetric Flue Gas Flow Rate, acfm 599,866.5 626,941.9 623,684.7 616,831.033

Percent Isokinetic of Sampling Rate, % 97.3 92.0 92.0 93.767

Percent Excess Air, % 83.9 83.9 83.9 83.900

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