Name: Mark Mediros

Title: Principal Engineer

Company: Taunton Municipal Light Plant

Sign Date: 11/24/2010

Name: Michael Kelley

Title: Project Manager

Company: CK Environmental, Inc

Sign Date: 11/24/2010

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.

Saturday, February 26, 2011 Page 1 of 34
11/24/2010

Facility Information:

Cleary Flood Station (TMLP)

1314 Somerset Avenue

Taunton MA 02780

Contact: Bill Lyons

Phone: 508-824-3166

Fax: 508-822-3782

Email: williamlyons@tmlp.com

Testing Company:

CK Environmental, Inc.

1020 Turnpike Street

Suite #8

Canton MA 02021

Contact:Michael Kelley

Phone: 781-828-5200

Fax: 781-828-5380

Email: mkelley@ckenvironmental.com

Air Permit Number:

01682

Permitted Source ID/Name:

Unit #8

Permitted Maximum Process Rate:

N/A

Max. Normal Operation Process Rate:

N/A

Target Process Test Rate

N/A

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

 process flow diagram:

Unit No. 8 is a 398 MMBtu/hr Combustion Engineering wall fired boiler. It has a gross generating capacity of 

approximately 29 megawatts (MW). Unit No. 8 is a peaking unit which fires 1 percent sulfur residual oil and small 

amounts of distillate oil when needed.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: FRS #: 110024570533

SCC / Description 10100405 External Combustion Boilers - Electric Generation - Residual Oil - Grade 5 Oil: 

Normal Firing 

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 Exit 106 0 0 106 1054 384 2 6

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Exit % H2O Method 1 - 4 3 180 0

Stack Exit Carbon Monoxide Method 10 3 120 0

Stack Exit Formaldehyde Method 0011 3 120 0

Stack Exit 2,3,7,8-TCDD Method 23 3 480 0

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

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

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

Saturday, February 26, 2011 Page 2 of 34
11/24/2010

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

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

Stack Exit OCDD Method 23 3 480 0

Stack Exit 2,3,7,8-TCDF Method 23 3 480 0

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

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

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

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

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

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

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

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

Stack Exit OCDF Method 23 3 480 0

Stack Exit Total Dioxins Method 23 3 480 0

Stack Exit Total Furans Method 23 3 480 0

Stack Exit 3,3',4,4'-TCB (PCB77) Method 23 3 480 0

Stack Exit 3,4,4',5-TCB (PCB81) Method 23 3 480 0

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

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

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

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

Stack Exit 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)

Stack Exit Method 23 3 480 0

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

Stack Exit 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 480 0

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

(PCB189)

Stack Exit Method 23 3 480 0

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 3 120 0

Stack Exit Hydrogen Chloride Method 26A 3 60 0

Stack Exit Hydrogen Fluoride Method 26A 3 60 0

Stack Exit Hydrogen Fluoride Method 26 3 60 0

Stack Exit Hydrogen Chloride Method 26 3 60 0

Total PM2.5 OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Filterable PM2.5 OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Inorganic (Aqueous) 

Condensible Part.

OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Organic Condensible 

Particulate

OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Stack Exit Cadmium Method 29 3 240 0

Stack Exit Copper Method 29 0

Stack Exit Silver Method 29 0

Stack Exit Chromium Method 29 3 240 0

Stack Exit Beryllium Method 29 3 240 0

Stack Exit Phosphorus (yellow or white) Method 29 0

Stack Exit Zinc Method 29 0

Stack Exit Arsenic Method 29 3 240 0

Saturday, February 26, 2011 Page 3 of 34
11/24/2010

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.

Stack Exit Selenium Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Mercury Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Lead Method 29 3 240 0

Stack Exit Barium Method 29 0

Stack Exit Co2 Method 3A CO2 3 120 0

Stack Exit O2 Method 3A O2 3 120 0

Stack Exit Sulfur Dioxide Method 6C 3 120 0

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

Saturday, February 26, 2011 Page 4 of 34
11/24/2010

Sampling / Stack Data Results Summary

Location Stack Exit - Method 0011

Average

Run Number Run # 3 Run #1 Run #2

Test Date 9/24/2010 9/24/2010 9/24/2010

Run Start Time 12:19:00 PM 7:32:00 

AM

9:51:00 AM

Run Finish Time 2:27:00 PM 9:41:00 

AM

11:59:00 AM

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 67.508 67.385 66.171 67.021

Moisture Content of Stack Gas, % 6.34 7.67 8.40 7.470

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

Carbon Dioxide, % 10.3 9.5 9.5 9.767

Oxygen, % 8.9 8.9 8.9 8.900

Average Stack Gas Temperature, °F 254.63 254.63 254.83 254.697

Dry Volumetric Flow Rate, dry scfm 59,599.9 59,000.5 58,623.4 59,074.600

Actual Wet Volumetric Flue Gas Flow Rate, acfm 85,526.6 85,857.5 86,041.3 85,808.467

Percent Isokinetic of Sampling Rate, % 108.3 109.2 107.9 108.467

F-Factor, dscfm/MMBtu @ %O2 9203 9203 9203 9,203.000

Fw 0 0 0 0.000

Fc 1399 1399 1399 1,399.000

Location Stack Exit - Method 10

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Saturday, February 26, 2011 Page 5 of 34
11/24/2010

Location Stack Exit - Method 23

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Location Stack Exit - Method 25A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Saturday, February 26, 2011 Page 6 of 34
11/24/2010

Location Stack Exit - Method 26A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Location Stack Exit - Method 29 

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Saturday, February 26, 2011 Page 7 of 34
11/24/2010

Location Stack Exit - Method 3A CO2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack Exit - Method 3A O2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Saturday, February 26, 2011 Page 8 of 34
11/24/2010

Location Stack Exit - Method 6C

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack Exit - Method 7E

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Saturday, February 26, 2011 Page 9 of 34
11/24/2010

Location Stack Exit - OTM - 27/28

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Saturday, February 26, 2011 Page 10 of 34
11/24/2010

Emissions Summary

Location: Stack Exit - Method 0011

Compound: Formaldehyde

Average

RunNumber Run #1 Run #2 Run # 3

Mass_mg 0.037 0.23 0.034 0.100

lb/mmBtuO2 1.94E-05 1.23E-04 1.78E-05 0.000

ppm 1.55E-02 9.83E-02 1.42E-02 0.043

ppm@7%O2 1.80E-02 1.14E-01 1.64E-02 0.049

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run Run #1 Run #2 Run #3

lb/mmBtuO2 5.61E-04 1.06E-03 3.13E-03 0.002

ppm 5.06E-01 9.50E-01 2.73E+00 1.395

ppm@7%O2 5.59E-01 1.06E+00 3.11E+00 1.576

Location: Stack Exit - Method 23

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

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.000000015 0.00000001 0.000000016 0.000

lb/mmBtuO2 2.15E-12 1.33E-12 2.22E-12 0.000

ng/dscm 2.20E-03 1.45E-03 2.38E-03 0.002

ng/dscm@7%O2 2.50E-03 1.54E-03 2.57E-03 0.002

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

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.00000004 0.000000021 0.000000023 0.000

lb/mmBtuO2 5.74E-12 2.79E-12 3.20E-12 0.000

ng/dscm 5.86E-03 3.04E-03 3.42E-03 0.004

ng/dscm@7%O2 6.65E-03 3.23E-03 3.70E-03 0.005

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

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.0000000087 0.0000000048 0.0000000028 0.000

lb/mmBtuO2 1.25E-12 6.38E-13 3.89E-13 0.000

ng/dscm 1.27E-03 6.95E-04 4.17E-04 0.001

ng/dscm@7%O2 1.44E-03 7.39E-04 4.51E-04 0.001

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

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.0000000018 0.0000000019 0.000000002 0.000

lb/mmBtuO2 2.58E-13 2.52E-13 2.78E-13 0.000

ng/dscm 2.64E-04 2.75E-04 2.98E-04 0.000

ng/dscm@7%O2 3.00E-04 2.92E-04 3.22E-04 0.000

Saturday, February 26, 2011 Page 11 of 34
11/24/2010

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

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.0000000022 0.000000008 0.000000008 0.000

lb/mmBtuO2 3.16E-13 1.06E-12 1.11E-12 0.000

ng/dscm 3.22E-04 1.16E-03 1.19E-03 0.001

ng/dscm@7%O2 3.65E-04 1.23E-03 1.29E-03 0.001

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

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.0000000016 0.0000000017 0.0000000019 0.000

lb/mmBtuO2 2.30E-13 2.26E-13 2.64E-13 0.000

ng/dscm 2.34E-04 2.46E-04 2.83E-04 0.000

ng/dscm@7%O2 2.66E-04 2.61E-04 3.06E-04 0.000

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

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.000000004 0.000000003 0.0000000031 0.000

lb/mmBtuO2 5.74E-13 3.99E-13 4.31E-13 0.000

ng/dscm 5.86E-04 4.34E-04 4.61E-04 0.000

ng/dscm@7%O2 6.65E-04 4.61E-04 4.98E-04 0.001

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

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.0000000016 0.0000000033 0.000000002 0.000

lb/mmBtuO2 2.30E-13 4.38E-13 2.78E-13 0.000

ng/dscm 2.34E-04 4.78E-04 2.98E-04 0.000

ng/dscm@7%O2 2.66E-04 5.08E-04 3.22E-04 0.000

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

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.0000000019 0.0000000024 0.0000000019 0.000

lb/mmBtuO2 2.73E-13 3.19E-13 2.64E-13 0.000

ng/dscm 2.78E-04 3.47E-04 2.83E-04 0.000

ng/dscm@7%O2 3.15E-04 3.69E-04 3.06E-04 0.000

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

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.0000000024 0.0000000019 0.0000000016 0.000

lb/mmBtuO2 3.44E-13 2.52E-13 2.22E-13 0.000

ng/dscm 3.51E-04 2.75E-04 2.38E-04 0.000

ng/dscm@7%O2 3.98E-04 2.92E-04 2.57E-04 0.000

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

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.000000003 0.0000000018 0.000000002 0.000

lb/mmBtuO2 4.31E-13 2.39E-13 2.78E-13 0.000

Saturday, February 26, 2011 Page 12 of 34
11/24/2010

ng/dscm 4.39E-04 2.61E-04 2.98E-04 0.000

ng/dscm@7%O2 4.98E-04 2.77E-04 3.22E-04 0.000

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

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.0000002 0.00000015 0.00000017 0.000

lb/mmBtuO2 2.87E-11 1.99E-11 2.36E-11 0.000

ng/dscm 2.93E-02 2.17E-02 2.53E-02 0.025

ng/dscm@7%O2 3.32E-02 2.31E-02 2.73E-02 0.028

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

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.00000014 0.00000012 0.00000013 0.000

lb/mmBtuO2 2.01E-11 1.59E-11 1.81E-11 0.000

ng/dscm 2.05E-02 1.74E-02 1.93E-02 0.019

ng/dscm@7%O2 2.33E-02 1.85E-02 2.09E-02 0.021

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

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.00000013 0.00000018 0.0000002 0.000

lb/mmBtuO2 1.87E-11 2.39E-11 2.78E-11 0.000

ng/dscm 1.90E-02 2.61E-02 2.98E-02 0.025

ng/dscm@7%O2 2.16E-02 2.77E-02 3.22E-02 0.027

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

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.00000014 0.00000012 0.00000013 0.000

lb/mmBtuO2 2.01E-11 1.59E-11 1.81E-11 0.000

ng/dscm 2.05E-02 1.74E-02 1.93E-02 0.019

ng/dscm@7%O2 2.33E-02 1.85E-02 2.09E-02 0.021

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

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.00000011 0.0000001 0.0000001 0.000

lb/mmBtuO2 1.58E-11 1.33E-11 1.39E-11 0.000

ng/dscm 1.61E-02 1.45E-02 1.49E-02 0.015

ng/dscm@7%O2 1.83E-02 1.54E-02 1.61E-02 0.017

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

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.00000045 0.00000056 0.00000067 0.000

lb/mmBtuO2 6.46E-11 7.44E-11 9.31E-11 0.000

ng/dscm 6.59E-02 8.11E-02 9.97E-02 0.082

ng/dscm@7%O2 7.48E-02 8.62E-02 1.08E-01 0.090

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

Average

RunNumber Run #1 Run #2 Run #3

Saturday, February 26, 2011 Page 13 of 34
11/24/2010

Mass_mg 0.00000011 0.00000011 0.0000001 0.000

lb/mmBtuO2 1.58E-11 1.46E-11 1.39E-11 0.000

ng/dscm 1.61E-02 1.59E-02 1.49E-02 0.016

ng/dscm@7%O2 1.83E-02 1.69E-02 1.61E-02 0.017

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

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.000000007 0.000000006 0.000000005 0.000

lb/mmBtuO2 1.00E-12 7.97E-13 6.95E-13 0.000

ng/dscm 1.02E-03 8.68E-04 7.44E-04 0.001

ng/dscm@7%O2 1.16E-03 9.22E-04 8.04E-04 0.001

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

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.0000000069 0.000000006 0.0000000064 0.000

lb/mmBtuO2 9.90E-13 7.97E-13 8.89E-13 0.000

ng/dscm 1.01E-03 8.68E-04 9.52E-04 0.001

ng/dscm@7%O2 1.15E-03 9.22E-04 1.03E-03 0.001

Compound: 2,3,7,8-TCDD

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.0000000026 0.0000000038 0.0000000024 0.000

lb/mmBtuO2 3.73E-13 5.05E-13 3.33E-13 0.000

ng/dscm 3.81E-04 5.50E-04 3.57E-04 0.000

ng/dscm@7%O2 4.32E-04 5.84E-04 3.86E-04 0.000

Compound: 2,3,7,8-TCDF

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.000000007 0.000000006 0.0000000049 0.000

lb/mmBtuO2 1.00E-12 7.97E-13 6.81E-13 0.000

ng/dscm 1.02E-03 8.68E-04 7.29E-04 0.001

ng/dscm@7%O2 1.16E-03 9.22E-04 7.88E-04 0.001

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

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.00000014 0.00000013 0.00000014 0.000

lb/mmBtuO2 2.01E-11 1.73E-11 1.94E-11 0.000

ng/dscm 2.05E-02 1.88E-02 2.08E-02 0.020

ng/dscm@7%O2 2.33E-02 2.00E-02 2.25E-02 0.022

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

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.00000011 0.00000011 0.0000001 0.000

lb/mmBtuO2 1.58E-11 1.46E-11 1.39E-11 0.000

ng/dscm 1.61E-02 1.59E-02 1.49E-02 0.016

ng/dscm@7%O2 1.83E-02 1.69E-02 1.61E-02 0.017

Saturday, February 26, 2011 Page 14 of 34
11/24/2010

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

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.00000014 0.00000013 0.00000017 0.000

lb/mmBtuO2 2.01E-11 1.73E-11 2.36E-11 0.000

ng/dscm 2.05E-02 1.88E-02 2.53E-02 0.022

ng/dscm@7%O2 2.33E-02 2.00E-02 2.73E-02 0.024

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

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.00000013 0.00000012 0.00000016 0.000

lb/mmBtuO2 1.87E-11 1.59E-11 2.22E-11 0.000

ng/dscm 1.90E-02 1.74E-02 2.38E-02 0.020

ng/dscm@7%O2 2.16E-02 1.85E-02 2.57E-02 0.022

Compound: OCDD

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.000000077 0.000000068 0.00000006 0.000

lb/mmBtuO2 1.10E-11 9.03E-12 8.34E-12 0.000

ng/dscm 1.13E-02 9.84E-03 8.93E-03 0.010

ng/dscm@7%O2 1.28E-02 1.05E-02 9.65E-03 0.011

Compound: OCDF

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.000000015 0.000000017 0.000000014 0.000

lb/mmBtuO2 2.15E-12 2.26E-12 1.94E-12 0.000

ng/dscm 2.20E-03 2.46E-03 2.08E-03 0.002

ng/dscm@7%O2 2.50E-03 2.61E-03 2.25E-03 0.002

Compound: Total Dioxins

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.0000001247 0.0000001055 0.0000001 0.000

lb/mmBtuO2 1.79E-11 1.40E-11 1.39E-11 0.000

ng/dscm 1.83E-02 1.53E-02 1.49E-02 0.016

ng/dscm@7%O2 2.08E-02 1.63E-02 1.61E-02 0.018

Compound: Total Furans

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.000000124 0.000000087 0.000000066 0.000

lb/mmBtuO2 1.78E-11 1.16E-11 9.17E-12 0.000

ng/dscm 1.82E-02 1.26E-02 9.82E-03 0.014

ng/dscm@7%O2 2.07E-02 1.34E-02 1.06E-02 0.015

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run Run #1 Run #2 Run #3

lb/mmBtuO2 9.65E-03 8.01E-03 8.02E-03 0.009

Saturday, February 26, 2011 Page 15 of 34
11/24/2010

ppm 5.48E+00 4.59E+00 4.60E+00 4.890

ppm@7%O2 6.10E+00 5.06E+00 5.07E+00 5.410

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 1.9 0.68 0.76 1.113

Elb/hr 1.68E-01 1.84E-01 1.96E-01 0.183

lb/mmBtuO2 7.75E-04 8.79E-04 8.81E-04 0.001

mg/dscm 8.15E-01 9.15E-01 9.32E-01 0.887

mg/dscm@7%O2 8.97E-01 1.02E+00 1.02E+00 0.979

Compound: Hydrogen Fluoride

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.25 0.2 0.2 0.217

Elb/hr 2.21E-02 5.40E-02 5.16E-02 0.043

lb/mmBtuO2 1.02E-04 2.59E-04 2.32E-04 0.000

mg/dscm 1.07E-01 2.69E-01 2.45E-01 0.207

mg/dscm@7%O2 1.18E-01 2.99E-01 2.68E-01 0.228

Location: Stack Exit - Method 29 

Compound: Arsenic

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.01004 0.01082 0.01183 0.011

Elb/hr 6.35E-04 6.78E-04 7.50E-04 0.001

lb/mmBtuO2 3.13E-06 3.13E-06 3.62E-06 0.000

mg/dscm 3.31E-03 3.28E-03 3.70E-03 0.003

mg/dscm@7%O2 3.62E-03 3.62E-03 4.19E-03 0.004

Compound: Barium

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.143 0.155 0.1125 0.137

Elb/hr 9.04E-03 9.71E-03 7.13E-03 0.009

lb/mmBtuO2 4.46E-05 4.49E-05 3.44E-05 0.000

mg/dscm 4.72E-02 4.70E-02 3.52E-02 0.043

mg/dscm@7%O2 5.16E-02 5.19E-02 3.99E-02 0.048

Compound: Beryllium

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.0012 0.0012 0.0012 0.001

Elb/hr 7.59E-05 7.52E-05 7.61E-05 0.000

lb/mmBtuO2 3.74E-07 3.47E-07 3.67E-07 0.000

mg/dscm 3.96E-04 3.64E-04 3.75E-04 0.000

mg/dscm@7%O2 4.33E-04 4.02E-04 4.25E-04 0.000

Compound: Cadmium

Average

RunNumber Run #1 Run #2 Run #3

Saturday, February 26, 2011 Page 16 of 34
11/24/2010

Mass_mg 0.00137 0.00161 0.00144 0.001

Elb/hr 8.67E-05 1.01E-04 9.13E-05 0.000

lb/mmBtuO2 4.27E-07 4.66E-07 4.41E-07 0.000

mg/dscm 4.52E-04 4.89E-04 4.50E-04 0.000

mg/dscm@7%O2 4.94E-04 5.40E-04 5.10E-04 0.001

Compound: Chromium

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.028 0.0493 0.0349 0.037

Elb/hr 1.77E-03 3.09E-03 2.21E-03 0.002

lb/mmBtuO2 8.72E-06 1.43E-05 1.07E-05 0.000

mg/dscm 9.24E-03 1.50E-02 1.09E-02 0.012

mg/dscm@7%O2 1.01E-02 1.66E-02 1.24E-02 0.013

Compound: Copper

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.0982 0.1026 0.1085 0.103

Elb/hr 6.21E-03 6.43E-03 6.88E-03 0.007

lb/mmBtuO2 3.06E-05 2.97E-05 3.32E-05 0.000

mg/dscm 3.24E-02 3.11E-02 3.39E-02 0.032

mg/dscm@7%O2 3.54E-02 3.43E-02 3.84E-02 0.036

Compound: Lead

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.0427 0.062 0.0392 0.048

Elb/hr 2.70E-03 3.88E-03 2.48E-03 0.003

lb/mmBtuO2 1.33E-05 1.79E-05 1.20E-05 0.000

mg/dscm 1.41E-02 1.88E-02 1.23E-02 0.015

mg/dscm@7%O2 1.54E-02 2.08E-02 1.39E-02 0.017

Compound: Manganese

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 4.3008 0.0509 0.21 1.521

Elb/hr 2.72E-01 3.19E-03 1.33E-02 0.096

lb/mmBtuO2 1.34E-03 1.47E-05 6.43E-05 0.000

mg/dscm 1.42E+00 1.54E-02 6.57E-02 0.500

mg/dscm@7%O2 1.55E+00 1.70E-02 7.45E-02 0.547

Compound: Mercury

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.0003596 0.0003739 0.0003329 0.000

Elb/hr 2.27E-05 2.34E-05 2.11E-05 0.000

lb/mmBtuO2 1.12E-07 1.08E-07 1.02E-07 0.000

mg/dscm 1.19E-04 1.13E-04 1.04E-04 0.000

mg/dscm@7%O2 1.30E-04 1.25E-04 1.18E-04 0.000

Compound: Nickel

Average

RunNumber Run #1 Run #2 Run #3

Saturday, February 26, 2011 Page 17 of 34
11/24/2010

Mass_mg 2.25 2.4132 2.245 2.303

Elb/hr 1.42E-01 1.51E-01 1.42E-01 0.145

lb/mmBtuO2 7.01E-04 6.98E-04 6.87E-04 0.001

mg/dscm 7.42E-01 7.32E-01 7.02E-01 0.725

mg/dscm@7%O2 8.11E-01 8.08E-01 7.96E-01 0.805

Compound: Phosphorus (yellow or white)

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.628 0.658 0.637 0.641

Elb/hr 3.97E-02 4.12E-02 4.04E-02 0.040

lb/mmBtuO2 1.96E-04 1.90E-04 1.95E-04 0.000

mg/dscm 2.07E-01 2.00E-01 1.99E-01 0.202

mg/dscm@7%O2 2.26E-01 2.21E-01 2.26E-01 0.224

Compound: Selenium

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.012 0.0127 0.0157 0.013

Elb/hr 7.59E-04 7.96E-04 9.95E-04 0.001

lb/mmBtuO2 3.74E-06 3.68E-06 4.81E-06 0.000

mg/dscm 3.96E-03 3.85E-03 4.91E-03 0.004

mg/dscm@7%O2 4.33E-03 4.25E-03 5.57E-03 0.005

Compound: Silver

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.00315 0.00333 0.00245 0.003

Elb/hr 1.99E-04 2.09E-04 1.55E-04 0.000

lb/mmBtuO2 9.81E-07 9.64E-07 7.50E-07 0.000

mg/dscm 1.04E-03 1.01E-03 7.66E-04 0.001

mg/dscm@7%O2 1.14E-03 1.12E-03 8.68E-04 0.001

Compound: Zinc

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 0.702 0.761 0.647 0.703

Elb/hr 4.44E-02 4.77E-02 4.10E-02 0.044

lb/mmBtuO2 2.19E-04 2.20E-04 1.98E-04 0.000

mg/dscm 2.32E-01 2.31E-01 2.02E-01 0.222

mg/dscm@7%O2 2.54E-01 2.55E-01 2.29E-01 0.246

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Run Run #1 Run #2 Run #3

Elb/hr 1.88E+02 1.94E+02 1.79E+02 187.000

lb/mmBtuO2 8.75E-01 8.94E-01 8.67E-01 0.879

mg/dscm 9.11E+02 9.39E+02 8.83E+02 911.000

mg/dscm@7%O2 1.01E+03 1.03E+03 1.00E+03 1,013.333

ppm 3.42E+02 3.53E+02 3.31E+02 342.000

ppm@7%O2 3.81E+02 3.89E+02 3.77E+02 382.333

Saturday, February 26, 2011 Page 18 of 34
11/24/2010

Process Run Data

Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run Run #1 Run #2 Run #3

Elb/hr 5.88E+01 5.93E+01 8.01E+01 66.067

lb/mmBtuO2 2.74E-01 2.73E-01 3.89E-01 0.312

mg/dscm 2.85E+02 2.87E+02 3.96E+02 322.667

mg/dscm@7%O2 3.17E+02 3.16E+02 4.50E+02 361.000

ppm 1.49E+02 1.50E+02 2.07E+02 168.667

ppm@7%O2 1.66E+02 1.65E+02 2.35E+02 188.667

Location: Stack Exit - OTM - 27/28

Compound: Filterable PM2.5

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 104.4 114.3 115.4 111.367

lb/mmBtuO2 3.59E-02 3.78E-02 3.90E-02 0.038

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 9.5 14 18 13.833

lb/mmBtuO2 3.27E-03 4.63E-03 6.08E-03 0.005

Compound: Organic Condensible Particulate

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 2.5 2.3 1.8 2.200

lb/mmBtuO2 8.61E-04 7.60E-04 6.08E-04 0.001

Compound: Total PM2.5

Average

RunNumber Run #1 Run #2 Run #3

Mass_mg 116.4 130.6 135.2 127.400

lb/mmBtuO2 4.01E-02 4.32E-02 4.57E-02 0.043

Saturday, February 26, 2011 Page 19 of 34
11/24/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Residual Oil Burned 0 1000 Gallons/hr 0

2 Residual Oil Burned 0 1000 Gallons/hr 0

3 Residual Oil Burned 0 1000 Gallons/hr 0

1 Average Heat Input 168 MMBtu/hr Methods 29, 25A, 

26A - 9/20/10

0

2 Average Heat Input 169 MMBtu/hr Methods 29, 23, 

25A - 9/21/10

0

3 Average Heat Input 172 MMBtu/hr Methods OTM27/28, 23, 031, 

10 - 9/22/10

0

1 Steam Output 0 1000 lb steam/hr 0

2 Steam Output 0 1000 lb steam/hr 0

3 Steam Output 0 1000 lb steam/hr 0

1 Synfuel Firing Rate 0 0

2 Synfuel Firing Rate 0 0

3 Synfuel Firing Rate 0 0

1 Petroleum Coke Firing Rate 0 0

2 Petroleum Coke Firing Rate 0 0

3 Petroleum Coke Firing Rate 0 0

1 Coal Gas Firing Rate 0 0

2 Coal Gas Firing Rate 0 0

3 Coal Gas Firing Rate 0 0

1 Fuel Oil Firing Rate 0 0

2 Fuel Oil Firing Rate 0 0

3 Fuel Oil Firing Rate 0 0

1 Flue Gas Flow Rate 0 dscfm 0

1 Pressure Drop Across FGD (if applicable) 0 in H20 0

1 FGD Scrubber Liquor pH 0 pH 0

1 FGD Scrubber Liquor Flow Rate 0 gal/min 0

1 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

1 Flue Gas Oxygen Content 0 % 0

1 Flue Gas Carbon Dioxide Content 0 % 0

1 Flue Gas Moisture Content 0 % 0

1 Flue Gas Sampling Point Temperature 0 Deg F 0

Saturday, February 26, 2011 Page 20 of 34
11/24/2010

1 Flue Gas Pressure 0 atm 0

1 Standard Pressure 0 atm 0

1 Standard Temperature 0 Deg F 0

1 Unit Gross Electrical Output 0 MW 0

1 Unit Net Electric Generation 0 MWh 0

1 MW 0 MW 0

2 Flue Gas Flow Rate 0 dscfm 0

2 Pressure Drop Across FGD (if applicable) 0 in H20 0

2 FGD Scrubber Liquor pH 0 pH 0

2 FGD Scrubber Liquor Flow Rate 0 gal/min 0

2 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

2 Flue Gas Oxygen Content 0 % 0

2 Flue Gas Carbon Dioxide Content 0 % 0

2 Flue Gas Moisture Content 0 % 0

2 Flue Gas Sampling Point Temperature 0 Deg F 0

2 Flue Gas Pressure 0 atm 0

2 Standard Pressure 0 atm 0

2 Standard Temperature 0 Deg F 0

2 Unit Gross Electrical Output 0 MW 0

2 Unit Net Electric Generation 0 MWh 0

2 MW 0 MW 0

3 Flue Gas Flow Rate 0 dscfm 0

3 Pressure Drop Across FGD (if applicable) 0 in H20 0

3 FGD Scrubber Liquor pH 0 pH 0

3 FGD Scrubber Liquor Flow Rate 0 gal/min 0

3 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

3 Flue Gas Oxygen Content 0 % 0

3 Flue Gas Carbon Dioxide Content 0 % 0

3 Flue Gas Moisture Content 0 % 0

3 Flue Gas Sampling Point Temperature 0 Deg F 0

3 Flue Gas Pressure 0 atm 0

3 Standard Pressure 0 atm 0

3 Standard Temperature 0 Deg F 0

3 Unit Gross Electrical Output 0 MW 0

3 Unit Net Electric Generation 0 MWh 0

Saturday, February 26, 2011 Page 21 of 34
11/24/2010

3 MW 0 MW 0

1 MW 15.6 MW Methods 29, 25A, 

26A - 9/20/10

0

2 MW 15.6 MW Methods 29, 23, 

25A - 9/21/10

0

3 MW 16 MW Methods OTM27/28, 23, 031, 

10 - 9/22/10

0

4 Residual Oil Burned 0 1000 Gallons/hr 0

4 Average Heat Input 173 MMBtu/hr Methods OTM27/28, 23 - 9/23/100

4 Steam Output 0 1000 lb steam/hr 0

4 Synfuel Firing Rate 0 0

4 Petroleum Coke Firing Rate 0 0

4 Coal Gas Firing Rate 0 0

4 Fuel Oil Firing Rate 0 0

4 Flue Gas Flow Rate 0 dscfm 0

4 Pressure Drop Across FGD (if applicable) 0 in H20 0

4 FGD Scrubber Liquor pH 0 pH 0

4 FGD Scrubber Liquor Flow Rate 0 gal/min 0

4 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

4 Flue Gas Oxygen Content 0 % 0

4 Flue Gas Carbon Dioxide Content 0 % 0

4 Flue Gas Moisture Content 0 % 0

4 Flue Gas Sampling Point Temperature 0 Deg F 0

4 Flue Gas Pressure 0 atm 0

4 Standard Pressure 0 atm 0

4 Standard Temperature 0 Deg F 0

4 Unit Gross Electrical Output 0 MW 0

4 Unit Net Electric Generation 0 MWh 0

4 MW 0 MW 0

4 MW 16 MW Methods OTM27/28, 23 - 9/23/100

5 Residual Oil Burned 0 1000 Gallons/hr 0

5 Average Heat Input 186 MMBtu/hr Methods 

RCRA011, 10 - 

9/24/10

0

5 Steam Output 0 1000 lb steam/hr 0

5 Synfuel Firing Rate 0 0

Saturday, February 26, 2011 Page 22 of 34
11/24/2010

APCD Run Data

Process Lab Run Data

5 Petroleum Coke Firing Rate 0 0

5 Coal Gas Firing Rate 0 0

5 Fuel Oil Firing Rate 0 0

5 Flue Gas Flow Rate 0 dscfm 0

5 Pressure Drop Across FGD (if applicable) 0 in H20 0

5 FGD Scrubber Liquor pH 0 pH 0

5 FGD Scrubber Liquor Flow Rate 0 gal/min 0

5 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

5 Flue Gas Oxygen Content 0 % 0

5 Flue Gas Carbon Dioxide Content 0 % 0

5 Flue Gas Moisture Content 0 % 0

5 Flue Gas Sampling Point Temperature 0 Deg F 0

5 Flue Gas Pressure 0 atm 0

5 Standard Pressure 0 atm 0

5 Standard Temperature 0 Deg F 0

5 Unit Gross Electrical Output 0 MW 0

5 Unit Net Electric Generation 0 MWh 0

5 MW 0 MW 0

5 MW 16.1 MW Methods 

RCRA011, 10 - 

9/24/10

0

Run Name Value UOM Comments

Target

Value

1 List all emissions control devices in order of 

process flow. Choose from

0 0

1 drop down lists. If not on list add description and 

provide detailed

0 0

1 desription in section 5a. 0 0

Run Name Value UOM Comments

1 See 4b Comments.(Refer to Fuel Analysis Spreadsheet) 0

Saturday, February 26, 2011 Page 23 of 34
11/24/2010

Sampling / Stack Data Results Detail

Location Stack Exit - Method 0011

Average

Run Number Run # 3 Run #1 Run #2

Test Date 9/24/2010 9/24/2010 9/24/2010

Run Start Time 12:19:00 PM 7:32:00 AM 9:51:00 AM

Run Finish Time 2:27:00 PM 9:41:00 AM 11:59:00 AM

Net Traversing Points 24 24 24

Net Run Time, minutes 120 120 120

Nozzle Diameter, inches 0.313 0.313 0.313 0.313

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.0207 1.0207 1.0207 1.021

Barometric Pressure, inches of Mercury 30.12 30.13 30.12 30.123

Average Orifice Meter Differential, inches H2O 0.90 0.90 0.90 0.900

Dry Gas Meter Volume Sampled, cubic feet 65.018 64.176 63.679 64.291

Average Dry Gas Meter Temperature, °F 63.67 58.00 63.25 61.640

Dry Gas Meter Volume Sampled, dscf 67.508 67.385 66.171 67.021

Total Moisture Liquid collected, g 97 119 129 115.000

Volume of Water Vapor, standard cubic feet 4.57 5.60 6.07 5.413

Moisture Content of Stack Gas, % 6.34 7.67 8.40 7.470

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

Dry Mole Fraction 0.9366 0.9233 0.916 0.925

Carbon Dioxide, % 10.3 9.5 9.5 9.767

Oxygen, % 8.9 8.9 8.9 8.900

Carbon Monoxide & Nitrogen, % 80.8 81.6 81.6 81.333

Fuel Factor 1.17 1.26 1.26

Dry Molecular Weight, lb/lb-Mole 30.00 29.88 29.88 29.920

Wet Molecular weight, lb/lb-Mole 29.24 28.97 28.88 29.030

Flue Gas Static Pressure, inches of H2O 0.08 0.08 0.08 0.080

Absolute Flue Gas Pressure, inches of Mercury 30.13 30.14 30.13 30.133

Average Stack Gas Temperature, °F 254.63 254.63 254.83 254.697

Average Velocity Head, inches of H2O 0.1293322494

25224

0.129189130

210234

0.129233774

694275

0.129

Average Stack Gas Velocity, feet/second 23.26 23.35 23.40 23.337

Stack Cross-Sectional Area, square feet 61.283 61.283 61.283 61.283

Dry Volumetric Flow Rate, dry scfm 59,599.9 59,000.5 58,623.4 59,074.600

Actual Wet Volumetric Flue Gas Flow Rate, acfm 85,526.6 85,857.5 86,041.3 85,808.467

Percent Isokinetic of Sampling Rate, % 108.3 109.2 107.9 108.467

Percent Excess Air, % 71.6 70.4 70.4 70.800

F-Factor, dscfm/MMBtu @ %O2 9203 9203 9203 9,203.000

Round Duct Diameter, inches 106 106 106

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 0 0 0 0.000

Fc 1399 1399 1399 1,399.000

Saturday, February 26, 2011 Page 24 of 34
11/24/2010

Location Stack Exit - Method 10

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Saturday, February 26, 2011 Page 25 of 34
11/24/2010

Location Stack Exit - Method 23

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Saturday, February 26, 2011 Page 26 of 34
11/24/2010

Location Stack Exit - Method 25A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Saturday, February 26, 2011 Page 27 of 34
11/24/2010

Location Stack Exit - Method 26A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Saturday, February 26, 2011 Page 28 of 34
11/24/2010

Location Stack Exit - Method 29 

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Saturday, February 26, 2011 Page 29 of 34
11/24/2010

Location Stack Exit - Method 3A CO2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Saturday, February 26, 2011 Page 30 of 34
11/24/2010

Location Stack Exit - Method 3A O2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Saturday, February 26, 2011 Page 31 of 34
11/24/2010

Location Stack Exit - Method 6C

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Saturday, February 26, 2011 Page 32 of 34
11/24/2010

Location Stack Exit - Method 7E

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Saturday, February 26, 2011 Page 33 of 34
11/24/2010

Location Stack Exit - OTM - 27/28

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Saturday, February 26, 2011 Page 34 of 34