Name: Roger Burger

Title: Site Business Manager

Company: TES Filer City Station Limited Partner

Sign Date: 9/1/2010

Name: Mark Horne

Title: Principal

Company: Environemntal Partners, Inc.

Sign Date: 9/1/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Filer City Station Section 114 Test Program - Unit 2 Boiler

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 24, 2011 Page 1 of 20
Filer City Station Section 114 Test Program - Unit 2 Boiler

9/1/2010

Facility Information:

TES Filer City Station. LP

700 Mee Street

Filer City MI 49634

Contact: Todd Guenthardt

Phone: 231-723-6573

Fax: 231-723-4766

Email: taguenthardt@cmsenergy.com

Testing Company:

Environmental Partners, Inc.

305 Hoover Boulevard

Suite 200

Holland MI 49423

Contact:Mark A, Horne, PE

Phone: 616-928-9128

Fax: 616-928-9126

Email: mark.horne@enviro-partners.com

Air Permit Number:

MI-ROP-N1685-2008a

Permitted Source ID/Name:

50835 EUBOILER02 (Boiler 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:

Boilers 1 is a spreader-stoker boilers fed with coal and any of the following fuels: wood and wood waste, 

construction demolition material, petroleum coke, tire derived fuel (TDF). The boiler utilizes a dry scrubber 

followed by a baghouse filter for particulate matter (PM) and sulfur dioxide (SO2) emissions control.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 2610100072 FRS #: 110000412054

SCC / Description 10100204 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Spreader Stoker (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

Boiler 2 76 0 0 0 152 608 6 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Boiler 1 Carbon Monoxide Method 10 3 120 0

Total organic compounds 

(TOC) as Propane

Boiler 1 Method 25A 3 120 0

Boiler 1 Co2 Method 3A CO2 3 120 0

Boiler 1 O2 Method 3A O2 3 120 0

Boiler 2 Carbon Monoxide Method 10 3 480 0

Regulation Description Compound Limit Unit

N/A - Optional information not included. 0

Thursday, February 24, 2011 Page 2 of 20
Filer City Station Section 114 Test Program - Unit 2 Boiler

9/1/2010

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 test report.

Boiler 2 2,3,7,8-TCDD Method 23 3 480 0

Boiler 2 1,2,3,7,8-PeCDD Method 23 3 480 0

Boiler 2 1,2,3,4,7,8-HxCDD Method 23 3 480 0

Boiler 2 1,2,3,6,7,8-HxCDD Method 23 3 480 0

Boiler 2 1,2,3,7,8,9-HxCDD Method 23 3 480 0

Boiler 2 1,2,3,4,6,7,8-HpCDD Method 23 3 480 0

Boiler 2 OCDD Method 23 3 480 0

Boiler 2 2,3,7,8-TCDF Method 23 3 480 0

Boiler 2 1,2,3,7,8-PeCDF Method 23 3 480 0

Boiler 2 2,3,4,7,8-PeCDF Method 23 3 480 0

Boiler 2 1,2,3,4,7,8-HxCDF Method 23 3 480 0

Boiler 2 1,2,3,6,7,8-HxCDF Method 23 3 480 0

Boiler 2 2,3,4,6,7,8-HxCDF Method 23 3 480 0

Boiler 2 1,2,3,7,8,9-HxCDF Method 23 3 480 0

Boiler 2 1,2,3,4,6,7,8-HpCDF Method 23 3 480 0

Boiler 2 1,2,3,4,7,8,9-HpCDF Method 23 3 480 0

Boiler 2 OCDF Method 23 3 480 0

Boiler 2 Other TCDD Method 23 3 480 0

Boiler 2 Other PeCDD Method 23 3 480 0

Boiler 2 Other HxCDD Method 23 3 480 0

Boiler 2 Other HpCDD Method 23 3 480 0

Boiler 2 Other TCDF Method 23 3 480 0

Boiler 2 Other PeCDF Method 23 3 480 0

Boiler 2 Other HxCDF Method 23 3 480 0

Boiler 2 Other HpCDF Method 23 3 480 0

Boiler 2 3,3',4,4'-TCB (PCB77) Method 23 3 480 0

Boiler 2 3,4,4',5-TCB (PCB81) Method 23 3 480 0

Boiler 2 2,3,3',4,4'-PeCB (PCB105) Method 23 3 480 0

Boiler 2 2,3,4,4',5-PeCB (PCB114) Method 23 3 480 0

Boiler 2 2,3',4,4',5-PeCB (PCB118) Method 23 3 480 0

Boiler 2 2',3,4,4',5-PeCB (PCB123) Method 23 3 480 0

Boiler 2 3,3',4,4',5-PeCB (PCB126) Method 23 3 480 0

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

HxCB (PCBs156/157)

Boiler 2 Method 23 3 480 0

Boiler 2 2,3',4,4',5,5'-HxCB (PCB167) Method 23 3 480 0

Boiler 2 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 480 0

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

(PCB189)

Boiler 2 Method 23 3 480 0

Total organic compounds 

(TOC) as Propane

Boiler 2 Method 25A 3 480 0

Boiler 2 Co2 Method 3A CO2 3 480 0

Boiler 2 O2 Method 3A O2 3 480 0

Thursday, February 24, 2011 Page 3 of 20
Filer City Station Section 114 Test Program - Unit 2 Boiler

9/1/2010

Sampling / Stack Data Results Summary

Location Boiler 2 - Method 1 - 4

Average

Run Number 1 2 3

Test Date 6/7/2010 6/8/2010 6/9/2010

Run Start Time 11:35:00 AM 8:40:00 

AM

8:00:00 AM

Run Finish Time 7:35:00 PM 4:40:00 PM 4:00:00 PM

Net Run Time, minutes 480 480 480

Dry Gas Meter Volume Sampled, dscf 429.222 435.784 431.987 432.331

Moisture Content of Stack Gas, % 10.95 10.92 11.28 11.050

Moisture Saturation at Stack Gas Temperature, % 55.82 58.57 57.83 57.407

Carbon Dioxide, % 13.757 13.462 13.255 13.491

Oxygen, % 5.8243 5.6203 5.4 5.615

Average Stack Gas Temperature, °F 183.21 185.50 184.29 184.333

Dry Volumetric Flow Rate, dry scfm 92,844.3 93,195.6 92,421.4 92,820.433

Actual Wet Volumetric Flue Gas Flow Rate, acfm 129,477.3 130,120.0 131,102.9 130,233.400

Percent Isokinetic of Sampling Rate, % 100.7 101.9 101.8 101.467

F-Factor, dscfm/MMBtu @ %O2 8411 9752 9789 9,317.333

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Boiler 2 - Method 10

Average

Run Number 1 2 3

Test Date 6/7/2010 6/8/2010 6/9/2010

Run Start Time 11:35:00 AM 8:40:00 

AM

8:00:00 AM

Run Finish Time 7:55:00 PM 4:50:00 PM 4:10:00 PM

Carbon Dioxide, % 13.757 13.462 13.255 13.491

Oxygen, % 5.8243 5.6203 5.4 5.615

Dry Volumetric Flow Rate, dry scfm 92844.3 93222.7 92421.4 92,829.467

F-Factor, dscfm/MMBtu @ %O2 8411 9752 9789 9,317.333

Moisture, % 10.95 10.92 11.28 11.050

Fuel Type

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Thursday, February 24, 2011 Page 4 of 20
Filer City Station Section 114 Test Program - Unit 2 Boiler

9/1/2010

Location Boiler 2 - Method 23

Average

Run Number 1 2 3

Test Date 6/7/2010 6/8/2010 6/9/2010

Run Start Time 11:35:00 AM 8:40:00 

AM

8:00:00 AM

Run Finish Time 7:35:00 PM 4:40:00 PM 4:00:00 PM

Net Run Time, minutes 480 480 480

Dry Gas Meter Volume Sampled, dscf 429.222 435.784 431.987 432.331

Moisture Content of Stack Gas, % 10.95 10.92 11.28 11.050

Moisture Saturation at Stack Gas Temperature, % 55.82 58.57 57.83 57.407

Carbon Dioxide, % 13.757 13.462 13.255 13.491

Oxygen, % 5.8243 5.6203 5.4 5.615

Average Stack Gas Temperature, °F 183.21 185.50 184.29 184.333

Dry Volumetric Flow Rate, dry scfm 92,844.3 93,195.6 92,421.4 92,820.433

Actual Wet Volumetric Flue Gas Flow Rate, acfm 129,477.3 130,120.0 131,102.9 130,233.400

Percent Isokinetic of Sampling Rate, % 100.7 101.9 101.8 101.467

F-Factor, dscfm/MMBtu @ %O2 8411 9752 9789 9,317.333

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Boiler 2 - Method 25A

Average

Run Number 1 2 3

Test Date 6/7/2010 6/8/2010 6/9/2010

Run Start Time 11:35:00 AM 8:40:00 

AM

8:00:00 AM

Run Finish Time 7:55:00 PM 4:50:00 PM 4:10:00 PM

Carbon Dioxide, % 13.757 13.462 13.255 13.491

Oxygen, % 5.8243 5.6203 5.4 5.615

Dry Volumetric Flow Rate, dry scfm 92844.3 93222.7 92421.4 92,829.467

F-Factor, dscfm/MMBtu @ %O2 8411 9752 9789 9,317.333

Moisture, % 10.95 10.92 11.28 11.050

Fuel Type

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Thursday, February 24, 2011 Page 5 of 20
Filer City Station Section 114 Test Program - Unit 2 Boiler

9/1/2010

Location Boiler 2 - Method 3A CO2

Average

Run Number 1 2 3

Test Date 6/7/2010 6/8/2010 6/9/2010

Run Start Time 11:35:00 AM 8:40:00 

AM

8:00:00 AM

Run Finish Time 7:35:00 PM 4:40:00 PM 4:00:00 PM

Carbon Dioxide, % 13.757 13.462 13.255 13.491

Oxygen, % 5.8243 5.6203 5.4 5.615

Dry Volumetric Flow Rate, dry scfm 92844.3 93222.7 92421.4 92,829.467

F-Factor, dscfm/MMBtu @ %O2 8411 9752 9789 9,317.333

Moisture, % 10.95 10.92 11.28 11.050

Fuel Type

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Boiler 2 - Method 3A O2

Average

Run Number 1 2 3

Test Date 6/7/2010 6/8/2010 6/9/2010

Run Start Time 11:35:00 AM 8:40:00 

AM

8:00:00 AM

Run Finish Time 7:35:00 PM 4:40:00 PM 4:00:00 PM

Carbon Dioxide, % 13.757 13.462 13.255 13.491

Oxygen, % 5.8243 5.6203 5.4 5.615

Dry Volumetric Flow Rate, dry scfm 92844.3 93222.7 92421.4 92,829.467

F-Factor, dscfm/MMBtu @ %O2 8411 9752 9789 9,317.333

Moisture, % 10.95 10.92 11.28 11.050

Fuel Type

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Thursday, February 24, 2011 Page 6 of 20
Filer City Station Section 114 Test Program - Unit 2 Boiler

9/1/2010

Emissions Summary

Location: Boiler 2 - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 4.32E-02 4.94E-02 6.56E-02 0.053

ppm 5.10E+01 5.09E+01 6.84E+01 56.767

ppm@7%O2 4.70E+01 4.63E+01 6.13E+01 51.533

Location: Boiler 2 - Method 23

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000987 0.0000000169 0.00000000735 0.000

lb/mmBtuO2 5.91E-13 1.14E-12 4.95E-13 0.000

ng/dscm 8.12E-04 1.37E-03 6.01E-04 0.001

ng/dscm@7%O2 7.49E-04 1.25E-03 5.39E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000579 0.0000000124 0.00000000607 0.000

lb/mmBtuO2 3.47E-13 8.37E-13 4.09E-13 0.000

ng/dscm 4.76E-04 1.01E-03 4.96E-04 0.001

ng/dscm@7%O2 4.39E-04 9.19E-04 4.45E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.000000003 0.00000000366 0.0000000019 0.000

lb/mmBtuO2 1.80E-13 2.47E-13 1.28E-13 0.000

ng/dscm 2.47E-04 2.97E-04 1.55E-04 0.000

ng/dscm@7%O2 2.28E-04 2.70E-04 1.39E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000151 0.00000000163 0.00000000133 0.000

lb/mmBtuO2 9.04E-14 1.10E-13 8.96E-14 0.000

ng/dscm 1.24E-04 1.32E-04 1.09E-04 0.000

ng/dscm@7%O2 1.14E-04 1.20E-04 9.77E-05 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000323 0.00000000494 0.00000000235 0.000

lb/mmBtuO2 1.93E-13 3.33E-13 1.58E-13 0.000

ng/dscm 2.66E-04 4.00E-04 1.92E-04 0.000

ng/dscm@7%O2 2.45E-04 3.64E-04 1.72E-04 0.000

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

Average

Thursday, February 24, 2011 Page 7 of 20
Filer City Station Section 114 Test Program - Unit 2 Boiler

9/1/2010

RunNumber 1 2 3

Mass_mg 0.00000000153 0.00000000188 0.00000000129 0.000

lb/mmBtuO2 9.16E-14 1.27E-13 8.69E-14 0.000

ng/dscm 1.26E-04 1.52E-04 1.05E-04 0.000

ng/dscm@7%O2 1.16E-04 1.38E-04 9.42E-05 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000234 0.0000000036 0.00000000126 0.000

lb/mmBtuO2 1.40E-13 2.43E-13 8.49E-14 0.000

ng/dscm 1.93E-04 2.92E-04 1.03E-04 0.000

ng/dscm@7%O2 1.78E-04 2.66E-04 9.24E-05 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000189 0.00000000274 0.00000000137 0.000

lb/mmBtuO2 1.13E-13 1.85E-13 9.23E-14 0.000

ng/dscm 1.56E-04 2.22E-04 1.12E-04 0.000

ng/dscm@7%O2 1.44E-04 2.02E-04 1.00E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000138 0.00000000148 0.00000000104 0.000

lb/mmBtuO2 8.27E-14 9.99E-14 7.01E-14 0.000

ng/dscm 1.14E-04 1.20E-04 8.50E-05 0.000

ng/dscm@7%O2 1.05E-04 1.09E-04 7.62E-05 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000149 0.00000000207 0.00000000126 0.000

lb/mmBtuO2 8.92E-14 1.40E-13 8.49E-14 0.000

ng/dscm 1.23E-04 1.68E-04 1.03E-04 0.000

ng/dscm@7%O2 1.13E-04 1.53E-04 9.24E-05 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000038 0.0000000113 0.00000000163 0.000

lb/mmBtuO2 2.28E-13 7.63E-13 1.10E-13 0.000

ng/dscm 3.13E-04 9.16E-04 1.33E-04 0.000

ng/dscm@7%O2 2.89E-04 8.33E-04 1.19E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000307 0.0000000055 0.00000000581 0.000

lb/mmBtuO2 1.84E-13 3.71E-13 3.91E-13 0.000

ng/dscm 2.53E-04 4.46E-04 4.75E-04 0.000

ng/dscm@7%O2 2.33E-04 4.06E-04 4.26E-04 0.000

Thursday, February 24, 2011 Page 8 of 20
Filer City Station Section 114 Test Program - Unit 2 Boiler

9/1/2010

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000601 0.00000004696 0.00000003289 0.000

lb/mmBtuO2 3.60E-12 3.17E-12 2.22E-12 0.000

ng/dscm 4.95E-03 3.81E-03 2.69E-03 0.004

ng/dscm@7%O2 4.56E-03 3.47E-03 2.41E-03 0.003

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

Average

RunNumber 1 2 3

Mass_mg 0.000000185 0.000000108 0.000000115 0.000

lb/mmBtuO2 1.11E-11 7.29E-12 7.75E-12 0.000

ng/dscm 1.52E-02 8.75E-03 9.40E-03 0.011

ng/dscm@7%O2 1.40E-02 7.96E-03 8.43E-03 0.010

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000165 0.0000000133 0.00000000958 0.000

lb/mmBtuO2 9.88E-13 8.98E-13 6.45E-13 0.000

ng/dscm 1.36E-03 1.08E-03 7.83E-04 0.001

ng/dscm@7%O2 1.25E-03 9.82E-04 7.02E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000156 0.00000000732 0.00000000627 0.000

lb/mmBtuO2 9.34E-13 4.94E-13 4.22E-13 0.000

ng/dscm 1.28E-03 5.93E-04 5.13E-04 0.001

ng/dscm@7%O2 1.18E-03 5.39E-04 4.60E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.000000437 0.000000241 0.000000272 0.000

lb/mmBtuO2 2.62E-11 1.63E-11 1.83E-11 0.000

ng/dscm 3.60E-02 1.95E-02 2.22E-02 0.026

ng/dscm@7%O2 3.32E-02 1.77E-02 1.99E-02 0.024

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000138 0.00000000568 0.0000000121 0.000

lb/mmBtuO2 8.27E-13 3.83E-13 8.15E-13 0.000

ng/dscm 1.14E-03 4.60E-04 9.89E-04 0.001

ng/dscm@7%O2 1.05E-03 4.18E-04 8.87E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000184 0.00000000171 0.00000000186 0.000

lb/mmBtuO2 1.10E-13 1.15E-13 1.25E-13 0.000

Thursday, February 24, 2011 Page 9 of 20
Filer City Station Section 114 Test Program - Unit 2 Boiler

9/1/2010

ng/dscm 1.51E-04 1.39E-04 1.52E-04 0.000

ng/dscm@7%O2 1.39E-04 1.26E-04 1.36E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000311 0.00000000773 0.00000000108 0.000

lb/mmBtuO2 1.86E-13 5.22E-13 7.28E-14 0.000

ng/dscm 2.56E-04 6.27E-04 8.83E-05 0.000

ng/dscm@7%O2 2.36E-04 5.70E-04 7.92E-05 0.000

Compound: 2,3,7,8-TCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000188 0.0000000209 0.00000000144 0.000

lb/mmBtuO2 1.13E-13 1.41E-12 9.70E-14 0.000

ng/dscm 1.55E-04 1.69E-03 1.18E-04 0.001

ng/dscm@7%O2 1.43E-04 1.54E-03 1.06E-04 0.001

Compound: 2,3,7,8-TCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000113 0.0000000584 0.00000000254 0.000

lb/mmBtuO2 6.77E-13 3.94E-12 1.71E-13 0.000

ng/dscm 9.30E-04 4.73E-03 2.08E-04 0.002

ng/dscm@7%O2 8.57E-04 4.30E-03 1.87E-04 0.002

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000349 0.00000000471 0.00000000332 0.000

lb/mmBtuO2 2.09E-13 3.18E-13 2.24E-13 0.000

ng/dscm 2.87E-04 3.82E-04 2.71E-04 0.000

ng/dscm@7%O2 2.65E-04 3.48E-04 2.43E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000066 0.00000000541 0.00000000438 0.000

lb/mmBtuO2 3.95E-13 3.65E-13 2.95E-13 0.000

ng/dscm 5.43E-04 4.38E-04 3.58E-04 0.000

ng/dscm@7%O2 5.01E-04 3.98E-04 3.21E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000537 0.0000000421 0.0000000481 0.000

lb/mmBtuO2 3.22E-12 2.84E-12 3.24E-12 0.000

ng/dscm 4.42E-03 3.41E-03 3.93E-03 0.004

ng/dscm@7%O2 4.08E-03 3.10E-03 3.52E-03 0.004

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

Average

RunNumber 1 2 3

Thursday, February 24, 2011 Page 10 of 20
Filer City Station Section 114 Test Program - Unit 2 Boiler

9/1/2010

Mass_mg 0.00000000414 0.00000000252 0.00000000318 0.000

lb/mmBtuO2 2.48E-13 1.70E-13 2.14E-13 0.000

ng/dscm 3.41E-04 2.04E-04 2.60E-04 0.000

ng/dscm@7%O2 3.14E-04 1.86E-04 2.33E-04 0.000

Compound: OCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000585 0.0000000832 0.0000000338 0.000

lb/mmBtuO2 3.50E-12 5.61E-12 2.28E-12 0.000

ng/dscm 4.81E-03 6.74E-03 2.76E-03 0.005

ng/dscm@7%O2 4.43E-03 6.13E-03 2.48E-03 0.004

Compound: OCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000134 0.0000000276 0.00000000652 0.000

lb/mmBtuO2 8.03E-13 1.86E-12 4.39E-13 0.000

ng/dscm 1.10E-03 2.24E-03 5.33E-04 0.001

ng/dscm@7%O2 1.01E-03 2.04E-03 4.78E-04 0.001

Compound: Other HpCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000842 0.0000000136 0.00000000673 0.000

lb/mmBtuO2 5.04E-13 9.18E-13 4.53E-13 0.000

ng/dscm 6.93E-04 1.10E-03 5.50E-04 0.001

ng/dscm@7%O2 6.39E-04 1.00E-03 4.93E-04 0.001

Compound: Other HpCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000000246 0.00000000257 0.00000000288 0.000

lb/mmBtuO2 1.47E-13 1.73E-13 1.94E-13 0.000

ng/dscm 2.02E-04 2.08E-04 2.35E-04 0.000

ng/dscm@7%O2 1.86E-04 1.89E-04 2.11E-04 0.000

Compound: Other HxCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000152 0.0000000153 0.00000000133 0.000

lb/mmBtuO2 9.10E-14 1.03E-12 8.96E-14 0.000

ng/dscm 1.25E-04 1.24E-03 1.09E-04 0.000

ng/dscm@7%O2 1.15E-04 1.13E-03 9.77E-05 0.000

Compound: Other HxCDF

Average

RunNumber 2 3 1

Mass_mg 0.0000000107 0.00000000785 0.0000000063 0.000

lb/mmBtuO2 7.22E-13 5.29E-13 3.77E-13 0.000

ng/dscm 8.67E-04 6.42E-04 5.18E-04 0.001

ng/dscm@7%O2 7.89E-04 5.76E-04 4.78E-04 0.001

Thursday, February 24, 2011 Page 11 of 20
Filer City Station Section 114 Test Program - Unit 2 Boiler

9/1/2010

Compound: Other PeCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000392 0.0000000103 0.00000000126 0.000

lb/mmBtuO2 2.35E-13 6.95E-13 8.49E-14 0.000

ng/dscm 3.23E-04 8.35E-04 1.03E-04 0.000

ng/dscm@7%O2 2.98E-04 7.60E-04 9.24E-05 0.000

Compound: Other PeCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000189 0.0000000279 0.0000000052 0.000

lb/mmBtuO2 1.13E-12 1.88E-12 3.50E-13 0.000

ng/dscm 1.56E-03 2.26E-03 4.25E-04 0.001

ng/dscm@7%O2 1.44E-03 2.06E-03 3.81E-04 0.001

Compound: Other TCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000678 0.0000000138 0.0000000116 0.000

lb/mmBtuO2 4.06E-13 9.31E-13 7.81E-13 0.000

ng/dscm 5.58E-04 1.12E-03 9.48E-04 0.001

ng/dscm@7%O2 5.14E-04 1.02E-03 8.50E-04 0.001

Compound: Other TCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000565 0.000000165 0.0000000209 0.000

lb/mmBtuO2 3.38E-12 1.11E-11 1.41E-12 0.000

ng/dscm 4.65E-03 1.34E-02 1.71E-03 0.007

ng/dscm@7%O2 4.29E-03 1.22E-02 1.53E-03 0.006

Compound: Total HpCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000183 0.0000000304 0.0000000141 0.000

lb/mmBtuO2 1.10E-12 2.05E-12 9.50E-13 0.000

ng/dscm 1.51E-03 2.46E-03 1.15E-03 0.002

ng/dscm@7%O2 1.39E-03 2.24E-03 1.03E-03 0.002

Compound: Total HpCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000000579 0.0000000124 0.00000000288 0.000

lb/mmBtuO2 3.47E-13 8.37E-13 1.94E-13 0.000

ng/dscm 4.76E-04 1.01E-03 2.35E-04 0.001

ng/dscm@7%O2 4.39E-04 9.19E-04 2.11E-04 0.001

Compound: Total HxCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000189 0.000000018 0 0.000

lb/mmBtuO2 1.13E-13 1.21E-12 0.00E+00 0.000

Thursday, February 24, 2011 Page 12 of 20
Filer City Station Section 114 Test Program - Unit 2 Boiler

9/1/2010

Process Run Data

ng/dscm 1.56E-04 1.46E-03 0.00E+00 0.001

ng/dscm@7%O2 1.44E-04 1.33E-03 0.00E+00 0.000

Compound: Total HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000137 0.0000000156 0.00000000972 0.000

lb/mmBtuO2 8.21E-13 1.05E-12 6.55E-13 0.000

ng/dscm 1.13E-03 1.26E-03 7.95E-04 0.001

ng/dscm@7%O2 1.04E-03 1.15E-03 7.13E-04 0.001

Compound: Total PeCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000392 0.0000000103 0 0.000

lb/mmBtuO2 2.35E-13 6.95E-13 0.00E+00 0.000

ng/dscm 3.23E-04 8.35E-04 0.00E+00 0.000

ng/dscm@7%O2 2.98E-04 7.60E-04 0.00E+00 0.000

Compound: Total PeCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000258 0.0000000469 0.0000000052 0.000

lb/mmBtuO2 1.55E-12 3.16E-12 3.50E-13 0.000

ng/dscm 2.12E-03 3.80E-03 4.25E-04 0.002

ng/dscm@7%O2 1.95E-03 3.46E-03 3.81E-04 0.002

Compound: Total TCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000678 0.0000000347 0.0000000116 0.000

lb/mmBtuO2 4.06E-13 2.34E-12 7.81E-13 0.000

ng/dscm 5.58E-04 2.81E-03 9.48E-04 0.001

ng/dscm@7%O2 5.14E-04 2.56E-03 8.50E-04 0.001

Compound: Total TCDF 

Average

RunNumber 1 2 3

Mass_mg 0.0000000678 0.000000223 0.0000000235 0.000

lb/mmBtuO2 4.06E-12 1.50E-11 1.58E-12 0.000

ng/dscm 5.58E-03 1.81E-02 1.92E-03 0.009

ng/dscm@7%O2 5.14E-03 1.65E-02 1.72E-03 0.008

Location: Boiler 2 - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 1.74E-03 1.12E-03 7.67E-04 0.001

ppm 1.30E+00 7.34E-01 5.08E-01 0.847

ppm@7%O2 1.20E+00 6.68E-01 4.56E-01 0.775

Thursday, February 24, 2011 Page 13 of 20
Filer City Station Section 114 Test Program - Unit 2 Boiler

9/1/2010

Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Boiler 2 Heat Input Million Btus/million BTU using O2 484.07 F-Factor 

Calculation

0

2 Boiler 2 Heat Input Million Btus/million BTU using O2 429.86 F-Factor 

Calculation

0

3 Boiler 2 Heat Input Million Btus/million BTU using O2 433.31 F-Factor 

Calculation

0

Run Name Value UOM Comments

Target

Value

1 Boiler 2 DRY SCRUBBER 17.8 gal lime slurry flow 0

2 Boiler 2 DRY SCRUBBER 22.8 gal lime slurry flow 0

3 Boiler 2 DRY SCRUBBER 18.1 gal lime slurry flow 0

1 Boiler 2 BAGHOUSE 7.15inches of water column 0

2 Boiler 2 BAGHOUSE 6.8inches of water column 0

3 Boiler 2 BAGHOUSE 6.9inches of water column 0

Run Name Value UOM Comments

1 Boiler 2 Fuel F-Factor 8301

2 Boiler 2 Fuel F-Factor 9513

3 Boiler 2 Fuel F-Factor 9491

Thursday, February 24, 2011 Page 14 of 20
Filer City Station Section 114 Test Program - Unit 2 Boiler

9/1/2010

Sampling / Stack Data Results Detail

Location Boiler 2 - Method 1 - 4

Average

Run Number 1 2 3

Test Date 6/7/2010 6/8/2010 6/9/2010

Run Start Time 11:35:00 AM 8:40:00 AM 8:00:00 AM

Run Finish Time 7:35:00 PM 4:40:00 PM 4:00:00 PM

Net Traversing Points 24 24 24

Net Run Time, minutes 480 480 480

Nozzle Diameter, inches 0.235 0.235 0.235 0.235

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.944 0.944 0.944 0.944

Barometric Pressure, inches of Mercury 29.4 29.45 29.05 29.300

Average Orifice Meter Differential, inches H2O 2.42 2.43 2.43 2.427

Dry Gas Meter Volume Sampled, cubic feet 467.600 476.840 481.230 475.223

Average Dry Gas Meter Temperature, °F 76.79 80.08 82.42 79.763

Dry Gas Meter Volume Sampled, dscf 429.222 435.784 431.987 432.331

Total Moisture Liquid collected, g 1121.5 1135 1167.5 1,141.333

Volume of Water Vapor, standard cubic feet 52.79 53.42 54.95 53.720

Moisture Content of Stack Gas, % 10.95 10.92 11.28 11.050

Moisture Saturation at Stack Gas Temperature, % 55.82 58.57 57.83 57.407

Dry Mole Fraction 0.8905 0.8908 0.8872 0.890

Carbon Dioxide, % 13.757 13.462 13.255 13.491

Oxygen, % 5.8243 5.6203 5.4 5.615

Carbon Monoxide & Nitrogen, % 80.4187 80.9177 81.345 80.894

Fuel Factor 1.10 1.14 1.17

Dry Molecular Weight, lb/lb-Mole 30.43 30.38 30.34 30.383

Wet Molecular weight, lb/lb-Mole 29.07 29.03 28.95 29.017

Flue Gas Static Pressure, inches of H2O -0.72 -0.52 -0.49 -0.577

Absolute Flue Gas Pressure, inches of Mercury 29.35 29.41 29.01 29.257

Average Stack Gas Temperature, °F 183.21 185.50 184.29 184.333

Average Velocity Head, inches of H2O 1.2071332336

7957

1.215513068

68232

1.216038456

24588

1.213

Average Stack Gas Velocity, feet/second 68.50 68.84 69.36 68.900

Stack Cross-Sectional Area, square feet 31.503 31.503 31.503 31.503

Dry Volumetric Flow Rate, dry scfm 92,844.3 93,195.6 92,421.4 92,820.433

Actual Wet Volumetric Flue Gas Flow Rate, acfm 129,477.3 130,120.0 131,102.9 130,233.400

Percent Isokinetic of Sampling Rate, % 100.7 101.9 101.8 101.467

Percent Excess Air, % 37.8 35.7 33.6 35.700

F-Factor, dscfm/MMBtu @ %O2 8411 9752 9789 9,317.333

Round Duct Diameter, inches 76 76 76

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Thursday, February 24, 2011 Page 15 of 20
Filer City Station Section 114 Test Program - Unit 2 Boiler

9/1/2010

Location Boiler 2 - Method 10

Average

Run Number 1 2 3

Test Date 6/7/2010 6/8/2010 6/9/2010

Run Start Time 11:35:00 AM 8:40:00 AM 8:00:00 AM

Run Finish Time 7:55:00 PM 4:50:00 PM 4:10:00 PM

Carbon Dioxide, % 13.757 13.462 13.255 13.491

Oxygen, % 5.8243 5.6203 5.4 5.615

Fuel Factor 1.1 1.14 1.17

Dry Volumetric Flow Rate, dry scfm 92844.3 93222.7 92421.4 92,829.467

F-Factor, dscfm/MMBtu @ %O2 8411 9752 9789 9,317.333

Moisture, % 10.95 10.92 11.28 11.050

Analyzer Make TECO TECO TECO

Analyzer Model 48C 48C 48C

Analyzer Serial Number

Operating Range

Operating Units ppm ppm ppm

No. Readings/Avg. 480 480 480 480.000

Calibration Set 21 22 23 22.000

Calibration Pre Zero Cylinder ID Zero Zero Zero

Calibration Pre Zero Cylinder Instrument Response 0.3 0 0.2 0.167

Calibration Pre Zero Cylinder Bias 0.2 -0.2 0.1 0.033

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CO Mid CO Mid CO Mid

Calibration Pre High Cylinder Instrument Response 51.9 51.5 51.6 51.667

Calibration Pre High Cylinder Bias 0.5 -0.4 0.1 0.067

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID Zero Zero Zero

Calibration Post Zero Cylinder Instrument Response -0.1 -0.2 0.1 -0.067

Calibration Post Zero Cylinder Bias -0.2 -0.4 0 -0.200

Calibration Post Zero Cylinder Drift 0.4 0.2 0.1 0.233

Calibration Post High Cylinder ID CO Mid CO Mid CO Mid

Calibration Post High Cylinder Instrument Response 51.2 51 51.9 51.367

Calibration Post High Cylinder Bias -0.2 -0.9 0.4 -0.233

Calibration Post High Cylinder Drift 0.7 0.5 0.3 0.500

Cavg 50.9 50.5 68.4 56.600

Cavg Units ppmvd ppmvd ppmvd

Cgas 51 50.9 68.4 56.767

Cgas Units ppmvd ppmvd ppmvd

Fuel Type

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Cgasw 0 0 0 0.000

Cgasw Units

Thursday, February 24, 2011 Page 16 of 20
Filer City Station Section 114 Test Program - Unit 2 Boiler

9/1/2010

Location Boiler 2 - Method 23

Average

Run Number 1 2 3

Test Date 6/7/2010 6/8/2010 6/9/2010

Run Start Time 11:35:00 AM 8:40:00 AM 8:00:00 AM

Run Finish Time 7:35:00 PM 4:40:00 PM 4:00:00 PM

Net Traversing Points 24 24 24

Net Run Time, minutes 480 480 480

Nozzle Diameter, inches 0.235 0.235 0.235 0.235

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.944 0.944 0.944 0.944

Barometric Pressure, inches of Mercury 29.4 29.45 29.05 29.300

Average Orifice Meter Differential, inches H2O 2.42 2.43 2.43 2.427

Dry Gas Meter Volume Sampled, cubic feet 467.600 476.840 481.230 475.223

Average Dry Gas Meter Temperature, °F 76.79 80.08 82.42 79.763

Dry Gas Meter Volume Sampled, dscf 429.222 435.784 431.987 432.331

Total Moisture Liquid collected, g 1121.5 1135 1167.5 1,141.333

Volume of Water Vapor, standard cubic feet 52.79 53.42 54.95 53.720

Moisture Content of Stack Gas, % 10.95 10.92 11.28 11.050

Moisture Saturation at Stack Gas Temperature, % 55.82 58.57 57.83 57.407

Dry Mole Fraction 0.8905 0.8908 0.8872 0.890

Carbon Dioxide, % 13.757 13.462 13.255 13.491

Oxygen, % 5.8243 5.6203 5.4 5.615

Carbon Monoxide & Nitrogen, % 80.4187 80.9177 81.345 80.894

Fuel Factor 1.10 1.14 1.17

Dry Molecular Weight, lb/lb-Mole 30.43 30.38 30.34 30.383

Wet Molecular weight, lb/lb-Mole 29.07 29.03 28.95 29.017

Flue Gas Static Pressure, inches of H2O -0.72 -0.52 -0.49 -0.577

Absolute Flue Gas Pressure, inches of Mercury 29.35 29.41 29.01 29.257

Average Stack Gas Temperature, °F 183.21 185.50 184.29 184.333

Average Velocity Head, inches of H2O 1.2071332336

7957

1.215513068

68232

1.216038456

24588

1.213

Average Stack Gas Velocity, feet/second 68.50 68.84 69.36 68.900

Stack Cross-Sectional Area, square feet 31.503 31.503 31.503 31.503

Dry Volumetric Flow Rate, dry scfm 92,844.3 93,195.6 92,421.4 92,820.433

Actual Wet Volumetric Flue Gas Flow Rate, acfm 129,477.3 130,120.0 131,102.9 130,233.400

Percent Isokinetic of Sampling Rate, % 100.7 101.9 101.8 101.467

Percent Excess Air, % 37.8 35.7 33.6 35.700

F-Factor, dscfm/MMBtu @ %O2 8411 9752 9789 9,317.333

Round Duct Diameter, inches 76 76 76

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Thursday, February 24, 2011 Page 17 of 20
Filer City Station Section 114 Test Program - Unit 2 Boiler

9/1/2010

Location Boiler 2 - Method 25A

Average

Run Number 1 2 3

Test Date 6/7/2010 6/8/2010 6/9/2010

Run Start Time 11:35:00 AM 8:40:00 AM 8:00:00 AM

Run Finish Time 7:55:00 PM 4:50:00 PM 4:10:00 PM

Carbon Dioxide, % 13.757 13.462 13.255 13.491

Oxygen, % 5.8243 5.6203 5.4 5.615

Fuel Factor 1.1 1.14 1.17

Dry Volumetric Flow Rate, dry scfm 92844.3 93222.7 92421.4 92,829.467

F-Factor, dscfm/MMBtu @ %O2 8411 9752 9789 9,317.333

Moisture, % 10.95 10.92 11.28 11.050

Analyzer Make JUM JUM JUM

Analyzer Model VE7 VE7 VE7

Analyzer Serial Number

Operating Range

Operating Units ppm ppm ppm

No. Readings/Avg. 480 480 480 480.000

Calibration Set 13 12 13 12.667

Calibration Pre Zero Cylinder ID Zero VOC Zero VOC Zero

Calibration Pre Zero Cylinder Instrument Response 0.2 0.1 0.2 0.167

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 VOC Mid VOC Mid VOC Mid

Calibration Pre High Cylinder Instrument Response 51.4 51.1 51.5 51.333

Calibration Pre High Cylinder Bias 0 -0.5 0 -0.167

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID Zero VOC Zero VOC Zero

Calibration Post Zero Cylinder Instrument Response 0.3 0 0.1 0.133

Calibration Post Zero Cylinder Bias 0.1 -0.1 -0.1 -0.033

Calibration Post Zero Cylinder Drift 0.1 0.1 0.1 0.100

Calibration Post High Cylinder ID VOC Mid VOC Mid VOC Mid

Calibration Post High Cylinder Instrument Response 51.1 51.4 51.7 51.400

Calibration Post High Cylinder Bias -0.3 -0.2 0.2 -0.100

Calibration Post High Cylinder Drift 0.3 0.3 0.2 0.267

Cavg 1.4 0.7 0.6 0.900

Cavg Units ppmvw ppmvw ppmvw

Cgas 1.3041 0.734 0.5077 0.849

Cgas Units ppmvd ppmvd ppmvd

Fuel Type

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Cgasw 1.1612745098

0392

0.653808593

75

0.450437317

784257

0.755

Cgasw Units ppmvw ppmvw ppmvw

Thursday, February 24, 2011 Page 18 of 20
Filer City Station Section 114 Test Program - Unit 2 Boiler

9/1/2010

Location Boiler 2 - Method 3A CO2

Average

Run Number 1 2 3

Test Date 6/7/2010 6/8/2010 6/9/2010

Run Start Time 11:35:00 AM 8:40:00 AM 8:00:00 AM

Run Finish Time 7:35:00 PM 4:40:00 PM 4:00:00 PM

Carbon Dioxide, % 13.757 13.462 13.255 13.491

Oxygen, % 5.8243 5.6203 5.4 5.615

Fuel Factor 0 0 1.17

Dry Volumetric Flow Rate, dry scfm 92844.3 93222.7 92421.4 92,829.467

F-Factor, dscfm/MMBtu @ %O2 8411 9752 9789 9,317.333

Moisture, % 10.95 10.92 11.28 11.050

Analyzer Make Servomex Servomex Servomex

Analyzer Model 1440C 1440C 1440C

Analyzer Serial Number

Operating Range 0 0.000

Operating Units % % %

No. Readings/Avg. 480 480 480 480.000

Calibration Set 51 52 53 52.000

Calibration Pre Zero Cylinder ID Zero Zero Zero

Calibration Pre Zero Cylinder Instrument Response 0.1 0.1 0.1 0.100

Calibration Pre Zero Cylinder Bias 0.42 0.42 0.42 0.420

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CO2 Mid CO2 Mid CO2 Mid

Calibration Pre High Cylinder Instrument Response 12.1 12 12.1 12.067

Calibration Pre High Cylinder Bias 0 0 0.42 0.140

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID Zero Zero Zero

Calibration Post Zero Cylinder Instrument Response 0.1 0 0.1 0.067

Calibration Post Zero Cylinder Bias 0.42 0 0.42 0.280

Calibration Post Zero Cylinder Drift 0 0 0 0.000

Calibration Post High Cylinder ID CO2 Mid CO2 Mid CO2 Mid

Calibration Post High Cylinder Instrument Response 12 11.9 12 11.967

Calibration Post High Cylinder Bias -0.42 -0.42 0 -0.280

Calibration Post High Cylinder Drift 0.42 0.42 0.42 0.420

Cavg 13.8 13.4 13.3 13.500

Cavg Units %vd %vd %vd

Cgas 13.7573 13.4622 13.2552 13.492

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

Thursday, February 24, 2011 Page 19 of 20
Filer City Station Section 114 Test Program - Unit 2 Boiler

9/1/2010

Location Boiler 2 - Method 3A O2

Average

Run Number 1 2 3

Test Date 6/7/2010 6/8/2010 6/9/2010

Run Start Time 11:35:00 AM 8:40:00 AM 8:00:00 AM

Run Finish Time 7:35:00 PM 4:40:00 PM 4:00:00 PM

Carbon Dioxide, % 13.757 13.462 13.255 13.491

Oxygen, % 5.8243 5.6203 5.4 5.615

Fuel Factor 1.1 1.14 1.17

Dry Volumetric Flow Rate, dry scfm 92844.3 93222.7 92421.4 92,829.467

F-Factor, dscfm/MMBtu @ %O2 8411 9752 9789 9,317.333

Moisture, % 10.95 10.92 11.28 11.050

Analyzer Make Servomex Servomex Servomex

Analyzer Model 1440C 1440C 1440

Analyzer Serial Number

Operating Range

Operating Units % % %

No. Readings/Avg. 480 480 480 480.000

Calibration Set 71 72 73 72.000

Calibration Pre Zero Cylinder ID Zero Zero Zero

Calibration Pre Zero Cylinder Instrument Response 0 0.1 0 0.033

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 O2 Mid O2 Mid O2 Mid

Calibration Pre High Cylinder Instrument Response 11.9 11.9 12 11.933

Calibration Pre High Cylinder Bias -0.4 -0.4 -0.4 -0.400

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID Zero Zero Zero

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 O2 Mid O2 Mid O2 Mid

Calibration Post High Cylinder Instrument Response 12 11.9 12 11.967

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

Calibration Post High Cylinder Drift 0.4 0 0 0.133

Cavg 5.8 5.6 5.4 5.600

Cavg Units %vd %vd %vd

Cgas 5.8243 5.6203 5.4 5.615

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

Thursday, February 24, 2011 Page 20 of 20