Name: William M. Swahl

Title: General Manager

Company: Exelon Generation Company, LLC

Sign Date: 9/3/2010

Name: Ken Hill

Title: Project Manager

Company: Weston Solution, Inc.

Sign Date: 9/3/2010

Permitted Facility Representative / Date Testing Company Representative / Date

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.

Friday, February 25, 2011 Page 1 of 25
9/3/2010

Facility Information:

Eddystone Generating Station

1 Industrial Highway

Eddystone PA 19022

Contact: Joe Kuklinski

Phone: 610-595-8113

Fax:

Email: joseph.kuklinski@exeloncorp.com

Testing Company:

Weston Solutions

1400 Weston Way

West Chester PA 19380

Contact: Ken Hill

Phone: 610-703043

Fax:

Email: k.hill@westonsolutions.com

Air Permit Number:

3161

Permitted Source ID/Name:

2 Unit 2

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

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

 process flow diagram:

See Attached Report

Industry/SCC/NAIS

Sampling Location Information:

Test Parameter Information:

AFS #: FRS #:

SCC / Description

The following state and federal regulations that apply to the proposed testing:

Location

Round

Duct

Diam.

Distance from 

upstream dist.

Distance from

downstream dist.

Number of

Traverse Ports

Equiv. 

Diam

Min.Travers 

Points

Rect. Duct 

Length /Width

Stack 276 0 0 0 1608 888 4 6

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Carbon Monoxide Method 10 3 0

Stack 2,3,7,8-TCDD Method 23 3 0

Stack 1,2,3,7,8-PeCDD Method 23 3 0

Stack 1,2,3,4,7,8-HxCDD Method 23 3 0

Stack 1,2,3,6,7,8-HxCDD Method 23 3 0

Stack 1,2,3,7,8,9-HxCDD Method 23 3 0

Stack 1,2,3,4,6,7,8-HpCDD Method 23 3 0

Stack OCDD Method 23 3 0

Friday, February 25, 2011 Page 2 of 25
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.

See Attached Report

Stack 2,3,7,8-TCDF Method 23 3 0

Stack 1,2,3,7,8-PeCDF Method 23 3 0

Stack 2,3,4,7,8-PeCDF Method 23 3 0

Stack 1,2,3,4,7,8-HxCDF Method 23 3 0

Stack 1,2,3,6,7,8-HxCDF Method 23 3 0

Stack 2,3,4,6,7,8-HxCDF Method 23 3 0

Stack 1,2,3,7,8,9-HxCDF Method 23 3 0

Stack 1,2,3,4,6,7,8-HpCDF Method 23 3 0

Stack 1,2,3,4,7,8,9-HpCDF Method 23 3 0

Stack OCDF Method 23 3 0

Stack 3,3',4,4'-TCB (PCB77) Method 23 3 0

Stack 3,4,4',5-TCB (PCB81) Method 23 3 0

Stack 2,3,3',4,4'-PeCB (PCB105) Method 23 3 0

Stack 2,3,4,4',5-PeCB (PCB114) Method 23 3 0

Stack 2,3',4,4',5-PeCB (PCB118) Method 23 3 0

Stack 2',3,4,4',5-PeCB (PCB123) Method 23 3 0

Stack 3,3',4,4',5-PeCB (PCB126) Method 23 3 0

2,3,3',4,4',5/2,3,3',4,4',5'-

HxCB (PCBs156/157)

Stack Method 23 3 0

Stack 2,3',4,4',5,5'-HxCB (PCB167) Method 23 3 0

Stack 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 0

2,3,3',4,4',5,5'-HpCB 

(PCB189)

Stack Method 23 3 0

Total organic compounds 

(TOC) as Propane

Stack Method 25A 3 0

Stack Hydrogen Chloride Method 26A 3 0

Stack Hydrogen Fluoride Method 26A 3 0

Stack Beryllium Method 29 3 0

Stack Phosphorus (yellow or white) Method 29 3 0

Stack Arsenic Method 29 3 0

Stack Cadmium Method 29 3 0

Stack Chromium Method 29 3 0

Stack Cobalt Method 29 3 0

Stack Filterable Particulate Method 29 3 0

Stack Lead Method 29 3 0

Stack Manganese Method 29 3 0

Stack Nickel Method 29 3 0

Stack Selenium Method 29 3 0

Stack Antimony Method 29 3 0

Stack Co2 Method 3A CO2 3 0

Stack O2 Method 3A O2 3 0

Organic Condensible 

Particulate

Stack Method 5/OTM-28 3 0

Inorganic (Aqueous) 

Condensible Part.

Stack Method 5/OTM-28 3 0

Stack Filterable Particulate Method 5/OTM-28 3 0

Friday, February 25, 2011 Page 3 of 25
9/3/2010

Friday, February 25, 2011 Page 4 of 25
9/3/2010

Sampling / Stack Data Results Summary

Location Stack - Method 10

Average

Run Number 1 2 3

Test Date 7/1/2010 7/2/2010 7/2/2010

Run Start Time 1:40:00 PM 7:36:00 

AM

10:38:00 AM

Run Finish Time 4:48:00 PM 10:05:00 

AM

1:09:00 PM

Carbon Dioxide, % 10.9 10.7 10.9 10.833

Oxygen, % 8.6 8.5 8.2 8.433

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack - Method 23

Average

Run Number 1 2 3

Test Date 6/29/2010 6/30/2010 7/1/2010

Run Start Time 9:30:00 AM 8:07:00 

AM

7:59:00 AM

Run Finish Time 6:24:00 PM 5:43:00 PM 5:05:00 PM

Net Run Time, minutes 480 480 480

Dry Gas Meter Volume Sampled, dscf 327.928 319.701 322.469 323.366

Moisture Content of Stack Gas, % 14.87 13.66 13.51 14.013

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

Carbon Dioxide, % 11.1 10.4 10.9 10.800

Oxygen, % 8.3 8.9 8.6 8.600

Average Stack Gas Temperature, °F 215.40 214.38 214.46 214.747

Dry Volumetric Flow Rate, dry scfm 943,636.4 946,770.5 936,003.1 942,136.667

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,417,437.9 1,413,200.1 1,399,489.4 1,410,042.46

7

Percent Isokinetic of Sampling Rate, % 100.7 97.9 99.9 99.500

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

Friday, February 25, 2011 Page 5 of 25
9/3/2010

Location Stack - Method 25A

Average

Run Number 1 2 3

Test Date 7/1/2010 7/2/2010 7/2/2010

Run Start Time 1:40:00 PM 7:36:00 

AM

10:38:00 AM

Run Finish Time 4:48:00 PM 10:05:00 

AM

1:09:00 PM

Carbon Dioxide, % 10.9 10.7 10.9 10.833

Oxygen, % 8.6 8.5 8.2 8.433

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 12.4 12.8 12.2 12.467

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack - Method 26A

Average

Run Number 1 2 3

Test Date 6/29/2010 6/29/2010 6/29/2010

Run Start Time 8:40:00 AM 11:08:00 

AM

1:34:00 PM

Run Finish Time 10:12:00 AM 12:47:00 

PM

3:04:00 PM

Net Run Time, minutes 60 60 60

Dry Gas Meter Volume Sampled, dscf 44.729 43.626 43.068 43.808

Moisture Content of Stack Gas, % 14.46 15.05 14.97 14.827

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

Carbon Dioxide, % 11.2 11.1 11.1 11.133

Oxygen, % 8.2 8.3 8.4 8.300

Average Stack Gas Temperature, °F 213.46 213.21 213.67 213.447

Dry Volumetric Flow Rate, dry scfm 945,226.4 947,362.7 938,134.6 943,574.567

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,408,962.2 1,421,426.5 1,407,217.2 1,412,535.30

0

Percent Isokinetic of Sampling Rate, % 105.2 105.9 105.5 105.533

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

Friday, February 25, 2011 Page 6 of 25
9/3/2010

Location Stack - Method 29

Average

Run Number 1 2 3

Test Date 6/30/2010 6/30/2010 7/1/2010

Run Start Time 8:07:00 AM 1:20:00 PM 7:59:00 AM

Run Finish Time 12:47:00 PM 5:59:00 PM 12:40:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 151.261 152.590 152.894 152.248

Moisture Content of Stack Gas, % 13.07 13.36 13.06 13.163

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

Carbon Dioxide, % 10.6 10.4 10.9 10.633

Oxygen, % 8.6 8.8 8.5 8.633

Average Stack Gas Temperature, °F 214.00 213.00 213.31 213.437

Dry Volumetric Flow Rate, dry scfm 952,220.1 949,776.1 955,578.2 952,524.800

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,398,741.5 1,397,744.4 1,406,718.6 1,401,068.16

7

Percent Isokinetic of Sampling Rate, % 102.3 103.5 103.0 102.933

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

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack - Method 3A CO2

Average

Run Number 1 2 3

Test Date 7/1/2010 7/2/2010 7/2/2010

Run Start Time 1:40:00 PM 7:36:00 

AM

10:38:00 AM

Run Finish Time 4:48:00 PM 10:05:00 

AM

1:09:00 PM

Carbon Dioxide, % 10.9 10.7 10.9 10.833

Oxygen, % 8.6 8.5 8.2 8.433

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000

Moisture, % 0 0 0 0.000

Fuel Type

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Friday, February 25, 2011 Page 7 of 25
9/3/2010

Location Stack - Method 3A O2

Average

Run Number 1 2 3

Test Date 7/1/2010 7/2/2010 7/2/2010

Run Start Time 1:40:00 PM 7:36:00 

AM

10:38:00 AM

Run Finish Time 4:48:00 PM 10:05:00 

AM

1:09:00 PM

Carbon Dioxide, % 10.9 10.7 10.9 10.833

Oxygen, % 8.6 8.5 8.2 8.433

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000

Moisture, % 0 0 0 0.000

Fuel Type

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Stack - Method 5/OTM-28

Average

Run Number 1 2 3

Test Date 6/30/2010 6/30/2010 7/1/2010

Run Start Time 8:07:00 AM 1:20:00 PM 7:59:00 AM

Run Finish Time 12:47:00 PM 5:59:00 PM 12:40:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 148.980 152.116 153.007 151.368

Moisture Content of Stack Gas, % 12.57 12.75 11.48 12.267

Moisture Saturation at Stack Gas Temperature, % 100.00 99.86 100.00 99.953

Carbon Dioxide, % 10.6 10.4 10.9 10.633

Oxygen, % 8.6 8.8 8.5 8.633

Average Stack Gas Temperature, °F 213.79 212.38 213.29 213.153

Dry Volumetric Flow Rate, dry scfm 953,897.9 956,149.8 970,042.1 960,029.933

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,392,758.6 1,395,999.4 1,402,480.8 1,397,079.60

0

Percent Isokinetic of Sampling Rate, % 102.4 104.3 103.4 103.367

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

Friday, February 25, 2011 Page 8 of 25
9/3/2010

Emissions Summary

Location: Stack - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 2.08E-02 2.00E-02 1.96E-02 0.020

ppm 1.72E+01 1.67E+01 1.68E+01 16.900

ppm@7%O2 1.94E+01 1.87E+01 1.84E+01 18.833

Location: Stack - Method 23

Compound: 1,2,3,4,6,7,8-HpCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000028 0.0000000036 0.0000000028 0.000

lb/mmBtuO2 3.05E-13 4.23E-13 3.18E-13 0.000

Compound: 1,2,3,4,6,7,8-HpCDF

Average

RunNumber 1 2 3

Mass_mg 0.000000002 0.0000000022 0.0000000019 0.000

lb/mmBtuO2 2.18E-13 2.58E-13 2.16E-13 0.000

Compound: 1,2,3,4,7,8,9-HpCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000018 0.0000000019 0.000000002 0.000

lb/mmBtuO2 1.96E-13 2.23E-13 2.27E-13 0.000

Compound: 1,2,3,4,7,8-HxCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000017 0.0000000018 0.0000000016 0.000

lb/mmBtuO2 1.85E-13 2.11E-13 1.82E-13 0.000

Compound: 1,2,3,4,7,8-HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000016 0.0000000017 0.0000000015 0.000

lb/mmBtuO2 1.74E-13 2.00E-13 1.70E-13 0.000

Compound: 1,2,3,6,7,8-HxCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000017 0.0000000018 0.0000000016 0.000

lb/mmBtuO2 1.85E-13 2.11E-13 1.82E-13 0.000

Compound: 1,2,3,6,7,8-HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000015 0.0000000016 0.0000000014 0.000

lb/mmBtuO2 1.64E-13 1.88E-13 1.59E-13 0.000

Friday, February 25, 2011 Page 9 of 25
9/3/2010

Compound: 1,2,3,7,8,9-HxCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000016 0.0000000017 0.0000000015 0.000

lb/mmBtuO2 1.74E-13 2.00E-13 1.70E-13 0.000

Compound: 1,2,3,7,8,9-HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000018 0.0000000019 0.0000000017 0.000

lb/mmBtuO2 1.96E-13 2.23E-13 1.93E-13 0.000

Compound: 1,2,3,7,8-PeCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000018 0.0000000016 0.0000000015 0.000

lb/mmBtuO2 1.96E-13 1.88E-13 1.70E-13 0.000

Compound: 1,2,3,7,8-PeCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000017 0.0000000018 0.0000000018 0.000

lb/mmBtuO2 1.85E-13 2.11E-13 2.05E-13 0.000

Compound: 2,3,3',4,4',5,5'-HpCB (PCB189)

Average

RunNumber 1 2 3

Mass_mg 0.000000003 0.000000004 0.0000000032 0.000

lb/mmBtuO2 3.27E-13 4.70E-13 3.64E-13 0.000

Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC

Average

RunNumber 1 2 3

Mass_mg 0.000000084 0.00000011 0.000000024 0.000

lb/mmBtuO2 9.16E-12 1.29E-11 2.73E-12 0.000

Compound: 2,3,3',4,4'-PeCB (PCB105)

Average

RunNumber 1 2 3

Mass_mg 0.00000052 0.00000055 0.00000013 0.000

lb/mmBtuO2 5.67E-11 6.46E-11 1.48E-11 0.000

Compound: 2,3',4,4',5,5'-HxCB (PCB167)

Average

RunNumber 1 2 3

Mass_mg 0.000000032 0.000000045 0.0000000078 0.000

lb/mmBtuO2 3.49E-12 5.29E-12 8.86E-13 0.000

Compound: 2,3,4,4',5-PeCB (PCB114)

Average

RunNumber 1 2 3

Mass_mg 0.000000038 0.000000039 0.0000000086 0.000

lb/mmBtuO2 4.14E-12 4.58E-12 9.77E-13 0.000

Friday, February 25, 2011 Page 10 of 25
9/3/2010

Compound: 2,3',4,4',5-PeCB (PCB118)

Average

RunNumber 1 2 3

Mass_mg 0.0000018 0.0000019 0.00000043 0.000

lb/mmBtuO2 1.96E-10 2.23E-10 4.89E-11 0.000

Compound: 2',3,4,4',5-PeCB (PCB123)

Average

RunNumber 1 2 3

Mass_mg 0.000000026 0.00000003 0.0000000072 0.000

lb/mmBtuO2 2.84E-12 3.52E-12 8.18E-13 0.000

Compound: 2,3,4,6,7,8-HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000017 0.0000000019 0.0000000018 0.000

lb/mmBtuO2 1.85E-13 2.23E-13 2.05E-13 0.000

Compound: 2,3,4,7,8-PeCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000017 0.0000000017 0.0000000017 0.000

lb/mmBtuO2 1.85E-13 2.00E-13 1.93E-13 0.000

Compound: 2,3,7,8-TCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000016 0.0000000018 0.0000000017 0.000

lb/mmBtuO2 1.74E-13 2.11E-13 1.93E-13 0.000

Compound: 2,3,7,8-TCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000021 0.0000000026 0.0000000031 0.000

lb/mmBtuO2 2.29E-13 3.05E-13 3.52E-13 0.000

Compound: 3,3',4,4',5,5'-HxCB (PCB169)

Average

RunNumber 1 2 3

Mass_mg 0.0000000032 0.000000003 0.0000000037 0.000

lb/mmBtuO2 3.49E-13 3.52E-13 4.20E-13 0.000

Compound: 3,3',4,4',5-PeCB (PCB126)

Average

RunNumber 1 2 3

Mass_mg 0.0000000054 0.000000011 0.0000000052 0.000

lb/mmBtuO2 5.89E-13 1.29E-12 5.91E-13 0.000

Compound: 3,3',4,4'-TCB (PCB77)

Average

RunNumber 1 2 3

Mass_mg 0.00000009 0.0000001 0.000000022 0.000

lb/mmBtuO2 9.82E-12 1.17E-11 2.50E-12 0.000

Friday, February 25, 2011 Page 11 of 25
9/3/2010

Compound: 3,4,4',5-TCB (PCB81)

Average

RunNumber 1 2 3

Mass_mg 0.0000000035 0.0000000034 0.0000000053 0.000

lb/mmBtuO2 3.82E-13 3.99E-13 6.02E-13 0.000

Compound: OCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000135 0.0000000163 0.000000011 0.000

lb/mmBtuO2 1.47E-12 1.91E-12 1.25E-12 0.000

Compound: OCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000034 0.000000005 0.0000000033 0.000

lb/mmBtuO2 3.71E-13 5.87E-13 3.75E-13 0.000

Location: Stack - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 5.44E-03 5.39E-03 4.39E-03 0.005

ppm 2.86E+00 2.85E+00 2.38E+00 2.697

ppm@7%O2 3.23E+00 3.19E+00 2.60E+00 3.007

Location: Stack - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 0.73 0.98 0.53 0.747

lb/mmBtuO2 5.79E-04 8.03E-04 4.44E-04 0.001

ppm 3.80E-01 5.23E-01 2.87E-01 0.397

ppm@7%O2 4.16E-01 5.77E-01 3.19E-01 0.437

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.25 0.25 0.25 0.250

lb/mmBtuO2 1.98E-04 2.05E-04 2.09E-04 0.000

ppm 2.37E-01 2.43E-01 2.46E-01 0.242

ppm@7%O2 2.59E-01 2.68E-01 2.74E-01 0.267

Location: Stack - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.0062 0.0064 0.0053 0.006

lb/mmBtuO2 1.50E-06 1.56E-06 1.26E-06 0.000

mg/dscm 1.45E-03 1.48E-03 1.22E-03 0.001

mg/dscm@7%O2 1.64E-03 1.70E-03 1.37E-03 0.002

Friday, February 25, 2011 Page 12 of 25
9/3/2010

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.05275 0.04095 0.02935 0.041

lb/mmBtuO2 1.28E-05 9.99E-06 6.98E-06 0.000

mg/dscm 1.23E-02 9.48E-03 6.78E-03 0.010

mg/dscm@7%O2 1.39E-02 1.09E-02 7.60E-03 0.011

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.00112 0.00097 0.00076 0.001

lb/mmBtuO2 2.71E-07 2.37E-07 1.81E-07 0.000

mg/dscm 2.62E-04 2.25E-04 1.76E-04 0.000

mg/dscm@7%O2 2.96E-04 2.58E-04 1.97E-04 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.001505 0.00177 0.0012 0.001

lb/mmBtuO2 3.65E-07 4.32E-07 2.85E-07 0.000

mg/dscm 3.51E-04 4.10E-04 2.77E-04 0.000

mg/dscm@7%O2 3.97E-04 4.71E-04 3.11E-04 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.01388 0.01421 0.01121 0.013

lb/mmBtuO2 3.36E-06 3.47E-06 2.66E-06 0.000

mg/dscm 3.24E-03 3.29E-03 2.59E-03 0.003

mg/dscm@7%O2 3.66E-03 3.78E-03 2.90E-03 0.003

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.002335 0.0022 0.00174 0.002

lb/mmBtuO2 5.66E-07 5.37E-07 4.14E-07 0.000

mg/dscm 5.45E-04 5.09E-04 4.02E-04 0.000

mg/dscm@7%O2 6.16E-04 5.85E-04 4.51E-04 0.001

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 48.9 54.3 39.3 47.500

lb/mmBtuO2 1.18E-02 1.33E-02 9.34E-03 0.011

mg/dscm 1.14E+01 1.26E+01 9.08E+00 11.027

mg/dscm@7%O2 1.29E+01 1.45E+01 1.02E+01 12.533

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.00906 0.0064 0.03041 0.015

lb/mmBtuO2 2.19E-06 1.56E-06 7.23E-06 0.000

Friday, February 25, 2011 Page 13 of 25
9/3/2010

mg/dscm 2.12E-03 1.48E-03 7.03E-03 0.004

mg/dscm@7%O2 2.40E-03 1.70E-03 7.88E-03 0.004

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.021 0.03296 0.02136 0.025

lb/mmBtuO2 5.09E-06 8.04E-06 5.08E-06 0.000

mg/dscm 4.90E-03 7.63E-03 4.93E-03 0.006

mg/dscm@7%O2 5.54E-03 8.77E-03 5.53E-03 0.007

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.01098 0.0103 0.0096 0.010

lb/mmBtuO2 2.66E-06 2.51E-06 2.28E-06 0.000

mg/dscm 2.56E-03 2.38E-03 2.22E-03 0.002

mg/dscm@7%O2 2.89E-03 2.73E-03 2.49E-03 0.003

Compound: Phosphorus (yellow or white)

Average

RunNumber 1 2 3

Mass_mg 0.246125 0.195 0.14005 0.194

lb/mmBtuO2 5.96E-05 4.76E-05 3.33E-05 0.000

mg/dscm 5.75E-02 4.51E-02 3.24E-02 0.045

mg/dscm@7%O2 6.50E-02 5.18E-02 3.63E-02 0.051

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.04295 0.0679 0.0582 0.056

lb/mmBtuO2 1.04E-05 1.66E-05 1.38E-05 0.000

mg/dscm 1.00E-02 1.57E-02 1.34E-02 0.013

mg/dscm@7%O2 1.13E-02 1.80E-02 1.50E-02 0.015

Location: Stack - Method 5/OTM-28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 46.8 60.3 46.4 51.167

lb/mmBtuO2 1.15E-02 1.48E-02 1.10E-02 0.012

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 18 20 13 17.000

lb/mmBtuO2 4.43E-03 4.90E-03 3.09E-03 0.004

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 1.1 1.1 1 1.067

lb/mmBtuO2 2.71E-04 2.69E-04 2.38E-04 0.000

Friday, February 25, 2011 Page 14 of 25
9/3/2010

Process Run Data

Friday, February 25, 2011 Page 15 of 25
9/3/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Gross Electric Output 261 MW Daily Average 

value,Run 1 

Dioxins, all runs of 

HCL

0

2 Gross Electric Output 259 MW Daily Average 

Value,Runs 1 & 2 

of m5/OTM28 & 

M5/29, Run 2 M23

0

3 Gross Electric Output 256 MW Daily average 

value, Runs 3 for 

M23, M5/OTM28, 

M29,Run1 of CO 

and THC

0

1 Steam Output 1780 klb/hr Run 1 Dioxins, all 

runs of HCL

0

2 Steam Output 1829 klb/hr Runs 1 & 2 of 

m5/OTM28 & 

M5/29, Run 2 M23

0

3 Steam Output 1837 klb/hr Runs 3 for M23, 

M5/OTM28, M29, 

Run1 of CO and 

THC

0

1 Total Heat Input 3280 mmbtu/hr Run 1 Dioxins, all 

runs of HCL

0

2 Total Heat Input 3330 mmbtu/hr Runs 1 & 2 of 

m5/OTM28 & 

M5/29, Run 2 M23

0

3 Total Heat Input 3305 mmbtu/hr Runs 3 for M23, 

M5/OTM28, M29, 

Run1 of CO and 

THC

0

1 Fuel Input Rate 2249 tons/day Run 1 Dioxins, all 

runs of HCL

0

2 Fuel Input Rate 2307 tons/day Runs 1 & 2 of 

m5/OTM28 & 

M5/29, Run 2 M23

0

3 Fuel Input Rate 2339 tons/day Runs 3 for M23, 

M5/OTM28, 

M29,Run1 of CO 

and THC

0

1 Net Electric Output 235 MW Daily average 

value,Run 1 

Dioxins, all runs of 

HCL

0

Friday, February 25, 2011 Page 16 of 25
9/3/2010

APCD Run Data

Process Lab Run Data

2 Net Electric Output 233 MW Daily average 

value,Runs 1 & 2 

of m5/OTM28 & 

M5/29, Run 2 M23

0

3 Net Electric Output 230 MW Daily average 

value, Runs 3 for 

M23, M5/OTM28, 

M29, Run1 of CO 

and THC

0

4 Gross Electric Output 139 MW Daily Value,Runs 

2 & 3 CO and THC

0

4 Steam Output 1749 klb/hr Runs 2 & 3 CO 

and THC

0

4 Total Heat Input 2851 mmbtu/hr Runs 2 & 3 CO 

and THC

0

4 Fuel Input Rate 2307 tons/day Runs 2 & 3 CO 

and THC

0

4 Net Electric Output 118 MW Daily Value,Runs 

2 & 3 CO and THC

0

Run Name Value UOM Comments

Target

Value

1 ELECTROSTATIC PRECIPITATOR 0 0

1 MECHANICAL COLLECTOR 0 0

1 SCRUBBER 0 0

1 SCRUBBER 0 0

Run Name Value UOM Comments

1 Coal Fuel Analysis 12077 Btu/lb

2 Coal Fuel Analysis 12268 Btu/lb

3 Coal Fuel Analysis 12002 Btu/lb

4 Coal Fuel Analysis 12267 Btu/lb

Friday, February 25, 2011 Page 17 of 25
9/3/2010

Sampling / Stack Data Results Detail

Location Stack - Method 10

Average

Run Number 1 2 3

Test Date 7/1/2010 7/2/2010 7/2/2010

Run Start Time 1:40:00 PM 7:36:00 AM 10:38:00 AM

Run Finish Time 4:48:00 PM 10:05:00 AM 1:09:00 PM

Carbon Dioxide, % 10.9 10.7 10.9 10.833

Oxygen, % 8.6 8.5 8.2 8.433

Fuel Factor 1.13 1.16 1.17

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 49.3 49.3 49.3 49.300

Operating Units PPM ppm ppm

No. Readings/Avg.

Calibration Set 5 6 6 5.667

Calibration Pre Zero Cylinder ID xc011677b xc011677b xc011677b

Calibration Pre Zero Cylinder Instrument Response 0.2 0.2 0.3 0.233

Calibration Pre Zero Cylinder Bias 0.41 0.41 0.61 0.477

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC281643 CC281643 CC281643

Calibration Pre High Cylinder Instrument Response 26 24.8 24.5 25.100

Calibration Pre High Cylinder Bias 2.23 1.62 1.01 1.620

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID xc011677b xc011677b xc011677b

Calibration Post Zero Cylinder Instrument Response 0.8 0.3 0.4 0.500

Calibration Post Zero Cylinder Bias 1.62 0.61 0.81 1.013

Calibration Post Zero Cylinder Drift 1.21 0.2 0.2 0.537

Calibration Post High Cylinder ID CC281643 CC281643 CC281643

Calibration Post High Cylinder Instrument Response 25.6 24.5 25.4 25.167

Calibration Post High Cylinder Bias 1.42 1.01 2.84 1.757

Calibration Post High Cylinder Drift 0.81 0.61 1.83 1.083

Cavg 18 16.6 16.9 17.167

Cavg Units ppmvd ppmvd ppmvd

Cgas 17.2233 16.685 16.7518 16.887

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

Friday, February 25, 2011 Page 18 of 25
9/3/2010

Location Stack - Method 23

Average

Run Number 1 2 3

Test Date 6/29/2010 6/30/2010 7/1/2010

Run Start Time 9:30:00 AM 8:07:00 AM 7:59:00 AM

Run Finish Time 6:24:00 PM 5:43:00 PM 5:05:00 PM

Net Traversing Points 96 96 96

Net Run Time, minutes 480 480 480

Nozzle Diameter, inches 0.234 0.234 0.234 0.234

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9976 0.9976 0.9976 0.998

Barometric Pressure, inches of Mercury 29.94 29.94 29.94 29.940

Average Orifice Meter Differential, inches H2O 1.85 1.83 1.81 1.830

Dry Gas Meter Volume Sampled, cubic feet 344.440 337.781 336.306 339.509

Average Dry Gas Meter Temperature, °F 96.14 94.21 85.22 91.857

Dry Gas Meter Volume Sampled, dscf 327.928 319.701 322.469 323.366

Total Moisture Liquid collected, g 1217 1074.4 1069.9 1,120.433

Volume of Water Vapor, standard cubic feet 57.28 50.57 50.36 52.737

Moisture Content of Stack Gas, % 14.87 13.66 13.51 14.013

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

Dry Mole Fraction 0.8513 0.8634 0.8649 0.860

Carbon Dioxide, % 11.1 10.4 10.9 10.800

Oxygen, % 8.3 8.9 8.6 8.600

Carbon Monoxide & Nitrogen, % 80.6 80.7 80.5 80.600

Fuel Factor 1.14 1.15 1.13

Dry Molecular Weight, lb/lb-Mole 30.11 30.02 30.09 30.073

Wet Molecular weight, lb/lb-Mole 28.31 28.38 28.46 28.383

Flue Gas Static Pressure, inches of H2O -0.14 -0.14 -0.14 -0.140

Absolute Flue Gas Pressure, inches of Mercury 29.93 29.93 29.93 29.930

Average Stack Gas Temperature, °F 215.40 214.38 214.46 214.747

Average Velocity Head, inches of H2O 0.7866414394

10522

0.784929758

100018

0.771849381

943573

0.781

Average Stack Gas Velocity, feet/second 56.86 56.69 56.14 56.563

Stack Cross-Sectional Area, square feet 415.476 415.476 415.476 415.476

Dry Volumetric Flow Rate, dry scfm 943,636.4 946,770.5 936,003.1 942,136.667

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,417,437.9 1,413,200.1 1,399,489.4 1,410,042.4

67

Percent Isokinetic of Sampling Rate, % 100.7 97.9 99.9 99.500

Percent Excess Air, % 64.0 71.7 68.0 67.900

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

Round Duct Diameter, inches 276 276 276

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

Friday, February 25, 2011 Page 19 of 25
9/3/2010

Location Stack - Method 25A

Average

Run Number 1 2 3

Test Date 7/1/2010 7/2/2010 7/2/2010

Run Start Time 1:40:00 PM 7:36:00 AM 10:38:00 AM

Run Finish Time 4:48:00 PM 10:05:00 AM 1:09:00 PM

Carbon Dioxide, % 10.9 10.7 10.9 10.833

Oxygen, % 8.6 8.5 8.2 8.433

Fuel Factor 1.13 1.16 1.17

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 12.4 12.8 12.2 12.467

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 84.4 84.4 84.4 84.400

Operating Units ppm ppm ppm

No. Readings/Avg.

Calibration Set 7 8 8 7.667

Calibration Pre Zero Cylinder ID xc011677b xc011677b xc011677b

Calibration Pre Zero Cylinder Instrument Response 0 0 0 0.000

Calibration Pre Zero Cylinder Bias 0 0 0 0.000

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID XC002134B XC002134B XC002134B

Calibration Pre High Cylinder Instrument Response 45.6 45.8 45.8 45.733

Calibration Pre High Cylinder Bias 0 0 0 0.000

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID xc011677b xc011677b xc011677b

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 0 0 0.000

Calibration Post High Cylinder ID XC002134B XC002134B XC002134B

Calibration Post High Cylinder Instrument Response 45.6 45.8 45.8 45.733

Calibration Post High Cylinder Bias 0 0 0 0.000

Calibration Post High Cylinder Drift 0 0 0 0.000

Cavg 2.5 2.5 2.1 2.367

Cavg Units ppmvw ppmvw ppmvw

Cgas 2.8604 2.8545 2.3814 2.699

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 2.5 2.489082969

43231

2.090829694

32314

2.360

Cgasw Units ppmvw ppmvw ppmvw

Friday, February 25, 2011 Page 20 of 25
9/3/2010

Location Stack - Method 26A

Average

Run Number 1 2 3

Test Date 6/29/2010 6/29/2010 6/29/2010

Run Start Time 8:40:00 AM 11:08:00 AM 1:34:00 PM

Run Finish Time 10:12:00 AM 12:47:00 PM 3:04:00 PM

Net Traversing Points 24 24 24

Net Run Time, minutes 60 60 60

Nozzle Diameter, inches 0.239 0.235 0.235 0.236

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9805 0.9805 0.9805 0.981

Barometric Pressure, inches of Mercury 29.94 29.94 29.94 29.940

Average Orifice Meter Differential, inches H2O 2.44 2.32 2.29 2.350

Dry Gas Meter Volume Sampled, cubic feet 46.525 45.883 45.465 45.958

Average Dry Gas Meter Temperature, °F 82.08 87.96 89.96 86.667

Dry Gas Meter Volume Sampled, dscf 44.729 43.626 43.068 43.808

Total Moisture Liquid collected, g 160.7 164.2 161.1 162.000

Volume of Water Vapor, standard cubic feet 7.56 7.73 7.58 7.623

Moisture Content of Stack Gas, % 14.46 15.05 14.97 14.827

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

Dry Mole Fraction 0.8554 0.8495 0.8503 0.852

Carbon Dioxide, % 11.2 11.1 11.1 11.133

Oxygen, % 8.2 8.3 8.4 8.300

Carbon Monoxide & Nitrogen, % 80.6 80.6 80.5 80.567

Fuel Factor 1.13 1.14 1.13

Dry Molecular Weight, lb/lb-Mole 30.12 30.11 30.11 30.113

Wet Molecular weight, lb/lb-Mole 28.37 28.29 28.30 28.320

Flue Gas Static Pressure, inches of H2O -0.15 -0.15 -0.15 -0.150

Absolute Flue Gas Pressure, inches of Mercury 29.93 29.93 29.93 29.930

Average Stack Gas Temperature, °F 213.46 213.21 213.67 213.447

Average Velocity Head, inches of H2O 0.7809763032

21328

0.792902778

532437

0.777056232

991907

0.784

Average Stack Gas Velocity, feet/second 56.52 57.02 56.45 56.663

Stack Cross-Sectional Area, square feet 415.476 415.476 415.476 415.476

Dry Volumetric Flow Rate, dry scfm 945,226.4 947,362.7 938,134.6 943,574.567

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,408,962.2 1,421,426.5 1,407,217.2 1,412,535.3

00

Percent Isokinetic of Sampling Rate, % 105.2 105.9 105.5 105.533

Percent Excess Air, % 62.7 64.0 65.4 64.033

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

Round Duct Diameter, inches 276 276 276

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

Friday, February 25, 2011 Page 21 of 25
9/3/2010

Location Stack - Method 29

Average

Run Number 1 2 3

Test Date 6/30/2010 6/30/2010 7/1/2010

Run Start Time 8:07:00 AM 1:20:00 PM 7:59:00 AM

Run Finish Time 12:47:00 PM 5:59:00 PM 12:40:00 PM

Net Traversing Points 48 48 48

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.222 0.222 0.222 0.222

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9849 0.9849 0.9849 0.985

Barometric Pressure, inches of Mercury 30.2 30.2 30.2 30.200

Average Orifice Meter Differential, inches H2O 1.47 1.51 1.50 1.493

Dry Gas Meter Volume Sampled, cubic feet 158.026 161.554 159.403 159.661

Average Dry Gas Meter Temperature, °F 85.23 92.60 82.35 86.727

Dry Gas Meter Volume Sampled, dscf 151.261 152.590 152.894 152.248

Total Moisture Liquid collected, g 483.2 499.9 488.1 490.400

Volume of Water Vapor, standard cubic feet 22.74 23.53 22.97 23.080

Moisture Content of Stack Gas, % 13.07 13.36 13.06 13.163

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

Dry Mole Fraction 0.8693 0.8664 0.8694 0.868

Carbon Dioxide, % 10.6 10.4 10.9 10.633

Oxygen, % 8.6 8.8 8.5 8.633

Carbon Monoxide & Nitrogen, % 80.8 80.8 80.6 80.733

Fuel Factor 1.16 1.16 1.14

Dry Molecular Weight, lb/lb-Mole 30.04 30.02 30.08 30.047

Wet Molecular weight, lb/lb-Mole 28.47 28.41 28.50 28.460

Flue Gas Static Pressure, inches of H2O -0.15 -0.15 -0.15 -0.150

Absolute Flue Gas Pressure, inches of Mercury 30.19 30.19 30.19 30.190

Average Stack Gas Temperature, °F 214.00 213.00 213.31 213.437

Average Velocity Head, inches of H2O 0.7785433824

8531

0.776946555

506045

0.789151906

835051

0.782

Average Stack Gas Velocity, feet/second 56.11 56.07 56.43 56.203

Stack Cross-Sectional Area, square feet 415.476 415.476 415.476 415.476

Dry Volumetric Flow Rate, dry scfm 952,220.1 949,776.1 955,578.2 952,524.800

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,398,741.5 1,397,744.4 1,406,718.6 1,401,068.1

67

Percent Isokinetic of Sampling Rate, % 102.3 103.5 103.0 102.933

Percent Excess Air, % 67.6 70.2 66.5 68.100

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

Round Duct Diameter, inches 276 276 276

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

Friday, February 25, 2011 Page 22 of 25
9/3/2010

Location Stack - Method 3A CO2

Average

Run Number 1 2 3

Test Date 7/1/2010 7/2/2010 7/2/2010

Run Start Time 1:40:00 PM 7:36:00 AM 10:38:00 AM

Run Finish Time 4:48:00 PM 10:05:00 AM 1:09:00 PM

Carbon Dioxide, % 10.9 10.7 10.9 10.833

Oxygen, % 8.6 8.5 8.2 8.433

Fuel Factor 1.13 1.16 1.17

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000

Moisture, % 0 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 16.9 16.9 16.9 16.900

Operating Units % % %

No. Readings/Avg.

Calibration Set 3 4 4 3.667

Calibration Pre Zero Cylinder ID xc011677b xc011677b xc011677b

Calibration Pre Zero Cylinder Instrument Response 0.1 -0.1 -0.1 -0.033

Calibration Pre Zero Cylinder Bias 0.59 -0.48 -0.48 -0.123

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID XC008875B 

CO2

XC008875B 

CO2

XC008875B 

CO2

Calibration Pre High Cylinder Instrument Response 8.8 8.7 8.9 8.800

Calibration Pre High Cylinder Bias -0.59 -0.48 0.48 -0.197

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID xc011677b xc011677b xc011677b

Calibration Post Zero Cylinder Instrument Response 0 -0.1 0 -0.033

Calibration Post Zero Cylinder Bias 0 -0.48 0 -0.160

Calibration Post Zero Cylinder Drift 0.59 0 0.48 0.357

Calibration Post High Cylinder ID XC008875B 

CO2

XC008875B 

CO2

XC008875B 

CO2

Calibration Post High Cylinder Instrument Response 8.8 8.9 8.8 8.833

Calibration Post High Cylinder Bias -0.59 0.48 0 -0.037

Calibration Post High Cylinder Drift 0 0.96 0.48 0.480

Cavg 10.6 10.5 10.7 10.600

Cavg Units %vd %vd %vd

Cgas 10.8514 10.7191 10.8708 10.814

Cgas Units %vd %vd %vd

Fuel Type

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Cgasw 0 0 0 0.000

Cgasw Units

Friday, February 25, 2011 Page 23 of 25
9/3/2010

Location Stack - Method 3A O2

Average

Run Number 1 2 3

Test Date 7/1/2010 7/2/2010 7/2/2010

Run Start Time 1:40:00 PM 7:36:00 AM 10:38:00 AM

Run Finish Time 4:48:00 PM 10:05:00 AM 1:09:00 PM

Carbon Dioxide, % 10.9 10.7 10.9 10.833

Oxygen, % 8.6 8.5 8.2 8.433

Fuel Factor 1.13 1.16 1.17

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000

Moisture, % 0 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 20.9 20.9 20.9 20.900

Operating Units % % %

No. Readings/Avg.

Calibration Set 1 2 2 1.667

Calibration Pre Zero Cylinder ID xc011677b xc011677b xc011677b

Calibration Pre Zero Cylinder Instrument Response 0.1 0 0 0.033

Calibration Pre Zero Cylinder Bias 0.48 0 0 0.160

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID XC008875B 

O2

XC008875B 

O2

XC008875B 

O2

Calibration Pre High Cylinder Instrument Response 11.8 12 11.9 11.900

Calibration Pre High Cylinder Bias -0.48 0.48 0 0.000

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID xc011677b xc011677b xc011677b

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 0.48 0 0 0.160

Calibration Post High Cylinder ID XC008875B 

O2

XC008875B 

O2

XC008875B 

O2

Calibration Post High Cylinder Instrument Response 11.8 11.9 11.9 11.867

Calibration Post High Cylinder Bias -0.48 0 0 -0.160

Calibration Post High Cylinder Drift 0 0.48 0 0.160

Cavg 8.5 8.5 8.2 8.400

Cavg Units %vd %vd %vd

Cgas 8.5579 8.4644 8.2 8.407

Cgas Units %vd %vd %vd

Fuel Type

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Cgasw 0 0 0 0.000

Cgasw Units

Friday, February 25, 2011 Page 24 of 25
9/3/2010

Location Stack - Method 5/OTM-28

Average

Run Number 1 2 3

Test Date 6/30/2010 6/30/2010 7/1/2010

Run Start Time 8:07:00 AM 1:20:00 PM 7:59:00 AM

Run Finish Time 12:47:00 PM 5:59:00 PM 12:40:00 PM

Net Traversing Points 48 48 48

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.22 0.22 0.22 0.220

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9805 0.9805 0.9805 0.981

Barometric Pressure, inches of Mercury 30.2 30.2 30.2 30.200

Average Orifice Meter Differential, inches H2O 1.73 1.79 1.81 1.777

Dry Gas Meter Volume Sampled, cubic feet 155.229 159.959 159.104 158.097

Average Dry Gas Meter Temperature, °F 81.69 86.77 78.92 82.460

Dry Gas Meter Volume Sampled, dscf 148.980 152.116 153.007 151.368

Total Moisture Liquid collected, g 455.1 472.2 421.5 449.600

Volume of Water Vapor, standard cubic feet 21.42 22.23 19.84 21.163

Moisture Content of Stack Gas, % 12.57 12.75 11.48 12.267

Moisture Saturation at Stack Gas Temperature, % 100.00 99.86 100.00 99.953

Dry Mole Fraction 0.8743 0.8725 0.8852 0.877

Carbon Dioxide, % 10.6 10.4 10.9 10.633

Oxygen, % 8.6 8.8 8.5 8.633

Carbon Monoxide & Nitrogen, % 80.8 80.8 80.6 80.733

Fuel Factor 1.16 1.16 1.14

Dry Molecular Weight, lb/lb-Mole 30.04 30.02 30.08 30.047

Wet Molecular weight, lb/lb-Mole 28.53 28.49 28.69 28.570

Flue Gas Static Pressure, inches of H2O -0.15 -0.15 -0.15 -0.150

Absolute Flue Gas Pressure, inches of Mercury 30.19 30.19 30.19 30.190

Average Stack Gas Temperature, °F 213.79 212.38 213.29 213.153

Average Velocity Head, inches of H2O 0.7737152659

83506

0.777957272

885652

0.789586959

220164

0.780

Average Stack Gas Velocity, feet/second 55.87 56.00 56.26 56.043

Stack Cross-Sectional Area, square feet 415.476 415.476 415.476 415.476

Dry Volumetric Flow Rate, dry scfm 953,897.9 956,149.8 970,042.1 960,029.933

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,392,758.6 1,395,999.4 1,402,480.8 1,397,079.6

00

Percent Isokinetic of Sampling Rate, % 102.4 104.3 103.4 103.367

Percent Excess Air, % 67.6 70.2 66.5 68.100

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

Round Duct Diameter, inches 276 276 276

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

Friday, February 25, 2011 Page 25 of 25