Name:

Title:

Company:

Sign Date:

Name:

Title:

Company:

Sign Date:

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.

Monday, March 07, 2011 Page 1 of 13
Facility Information:

Enter Plant Name (as reported U.S. DOE/EI

Enter physical Address

Enter physical city

Contact: Person to contact for more detail

Phone: Of above person

Fax: Of above person

Email: Of above person

Testing Company:

Name of primary testing organization

US postal address of above

US postal address of abov

Contact: Field test leader

Phone: Of above person

Fax: Of above person

Email: Of above person

Air Permit Number:

Enter your facilities ORIS Number here

Permitted Source ID/Name:

SJ9 Enter the Boiler ID of the tested boiler (left)

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:

This description should describe the process and associated controls to differentiate this facility from, or document 

similarity with others of same SCC.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: Enter ARS ID FRS #: Enter FRS ID

SCC / Description 10100404 External Combustion Boilers - Electric Generation - Residual Oil - Grade 6 Oil: 

Tangential 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 0 0 0 0 0 0 0 0

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

Monday, March 07, 2011 Page 2 of 13
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 Other TCDD Method 23 0

Stack Exit Other PeCDD Method 23 0

Stack Exit Other HxCDD Method 23 0

Stack Exit Other HpCDD Method 23 0

Stack Exit Other TCDF Method 23 0

Stack Exit Other PeCDF Method 23 0

Stack Exit Other HxCDF Method 23 0

Stack Exit Other HpCDF Method 23 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

Stack Exit Total PCBs Method 23 3 480 0

Stack Exit Total TEQ Method 23 3 480 0

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 3 120 0

Stack Exit Hydrogen Chloride Method 26 3 180 0

Stack Exit Hydrogen Fluoride Method 26 3 180 0

Stack Exit Hydrogen Chloride Method 26A 3 180 0

Stack Exit Hydrogen Fluoride Method 26A 3 180 0

Inorganic (Aqueous) 

Condensible Part.

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

Organic Condensible 

Particulate

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Monday, March 07, 2011 Page 3 of 13
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.

In this section, identify the promulgation date of any specified test method that you use for determining the 

procedures followed. This field is also used to document any modifications that are necessary to conduct the 

emissions test if they are outside the requirements of the cited method. If this modification was approved verbally by 

a regulatory agency, the name and date of approval should be included. Written formal approval should be attached 

to this file using the "Attach File" button. Test procedures that are different from those published in the Federal 

Register should be attached using the "Attach File" button.

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Stack Exit Arsenic Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Selenium Method 29 3 240 0

Stack Exit Lead Method 29 3 240 0

Stack Exit Chromium Method 29 3 240 0

Stack Exit Cadmium Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Beryllium Method 29 3 240 0

Stack Exit Filterable Particulate Method 29 3 240 0

Stack Exit Antimony Method 29 3 240 0

Stack Exit Co2 Method 3A CO2 3 120 0

Stack Exit Co2 Method 3A CO2 3 240 0

Stack Exit O2 Method 3A O2 3 240 0

Stack Exit O2 Method 3A O2 3 480 0

Stack Exit Co2 Method 3A CO2 3 480 0

Stack Exit O2 Method 3A O2 3 120 0

Inorganic (Aqueous) 

Condensible Part.

Method 5/OTM-28 3 240 0 Use only for wet 

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Organic Condensible 

Particulate

Method 5/OTM-28 3 240 0 Use only for wet 

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Total Particulate Method 5/OTM-28 3 240 0 Use only for wet 

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Stack Exit Filterable Particulate Method 5 3 240 0

Filterable Particulate Method 5/OTM-28 3 240 0 Use only for wet 

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Stack Exit Sulfur Dioxide Method 6C 3 180 0

Stack Exit Nitrogen oxides (NOx) Method 7E 3 180 0

Monday, March 07, 2011 Page 4 of 13
Sampling / Stack Data Results Summary

Location Stack Exit - Method 23

Average

Run Number 1 2 3

Test Date 10/15/2010 10/16/2010 10/17/2010

Run Start Time 9:04:00 AM 8:55:00 

AM

Run Finish Time 5:04:00 PM 5:10:00 PM

Net Run Time, minutes 480 480

Dry Gas Meter Volume Sampled, dscf 211.617 212.507 212.062

Moisture Content of Stack Gas, % 10.70 0.00 5.350

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.000

Carbon Dioxide, % 10.5 10.3 10.400

Oxygen, % 7.8 8.1 7.950

Average Stack Gas Temperature, °F 290.13 290.38

Dry Volumetric Flow Rate, dry scfm 0.0 0.0 0.000

Actual Wet Volumetric Flue Gas Flow Rate, acfm 0.0 0.0 0.000

Percent Isokinetic of Sampling Rate, % 100.7 90.5 95.600

F-Factor, dscfm/MMBtu @ %O2 9190 9190 0 6,126.667

Fw 10320 10320 0 6,880.000

Fc 1420 1420 0 946.667

Monday, March 07, 2011 Page 5 of 13
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

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

Monday, March 07, 2011 Page 6 of 13
Emissions Summary

Process Run Data

Location: Stack Exit - Method 23

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000025 0 0 0.000

lb/mmBtuO2 #Num!

ng/dscm #Num!

ng/dscm@7%O2 #Num!

Monday, March 07, 2011 Page 7 of 13
Process Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input 0 Million Btus 0

1 Average Heat Input 992 MMBtu/hr 0

1 Steam Output 718 1000 lb steam/hr 0

1 Synfuel Firing Rate 0 0

1 Petroleum Coke Firing Rate 0 0

1 Coal Gas Firing Rate 0 0

1 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

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 92 MW 0

1 Unit Net Electric Generation 0 MWh 0

2 Heat Input 0 Million Btus 0

2 Average Heat Input 992 MMBtu/hr 0

2 Steam Output 718 1000 lb steam/hr 0

2 Synfuel Firing Rate 0 0

2 Petroleum Coke Firing Rate 0 0

2 Coal Gas Firing Rate 0 0

2 Fuel Oil Firing Rate 0 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

Monday, March 07, 2011 Page 8 of 13
APCD Run Data

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 92 MW 0

2 Unit Net Electric Generation 0 MWh 0

3 Heat Input 0 Million Btus 0

3 Average Heat Input 992 MMBtu/hr 0

3 Steam Output 718 1000 lb steam/hr 0

3 Synfuel Firing Rate 0 0

3 Petroleum Coke Firing Rate 0 0

3 Coal Gas Firing Rate 0 0

3 Fuel Oil Firing Rate 0 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 92 MW 0

3 Unit Net Electric Generation 0 MWh 0

Run Name Value UOM Comments

Target

Value

1 List all emissions control devices in order of 0 0

Monday, March 07, 2011 Page 9 of 13
Process Lab Run Data

process flow. Choose from

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. 0

Monday, March 07, 2011 Page 10 of 13
Sampling / Stack Data Results Detail

Location Stack Exit - Method 23

Average

Run Number 1 2 3

Test Date 10/15/2010 10/16/2010 10/17/2010

Run Start Time 9:04:00 AM 8:55:00 AM

Run Finish Time 5:04:00 PM 5:10:00 PM

Net Traversing Points 49 49 1

Net Run Time, minutes 480 480

Nozzle Diameter, inches 0.18 0.18 0.180

Pitot Tube Coefficient 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.985 0.985 0.985

Barometric Pressure, inches of Mercury 29.8 29.75 29.775

Average Orifice Meter Differential, inches H2O 0.62 0.64

Dry Gas Meter Volume Sampled, cubic feet 223.227 224.051 0.000 149.093

Average Dry Gas Meter Temperature, °F 87.25 86.08

Dry Gas Meter Volume Sampled, dscf 211.617 212.507 212.062

Total Moisture Liquid collected, g 538.6 0 0 179.533

Volume of Water Vapor, standard cubic feet 25.35 0.00 0.00 8.450

Moisture Content of Stack Gas, % 10.70 0.00 5.350

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.000

Dry Mole Fraction 0.893 1 0.947

Carbon Dioxide, % 10.5 10.3 10.400

Oxygen, % 7.8 8.1 7.950

Carbon Monoxide & Nitrogen, % 81.7 81.6 81.650

Fuel Factor 1.25 1.24

Dry Molecular Weight, lb/lb-Mole 29.99 29.97

Wet Molecular weight, lb/lb-Mole 28.71 29.97 29.340

Flue Gas Static Pressure, inches of H2O 1 1 1.000

Absolute Flue Gas Pressure, inches of Mercury 29.87 29.82

Average Stack Gas Temperature, °F 290.13 290.38

Average Velocity Head, inches of H2O 0.9604088321

41769

0.999856844

071748

0.980

Average Stack Gas Velocity, feet/second 65.82 65.80 65.810

Stack Cross-Sectional Area, square feet 0.000 0.000 0.000 0.000

Dry Volumetric Flow Rate, dry scfm 0.0 0.0 0.000

Actual Wet Volumetric Flue Gas Flow Rate, acfm 0.0 0.0 0.000

Percent Isokinetic of Sampling Rate, % 100.7 90.5 95.600

Percent Excess Air, % 56.6 60.3

F-Factor, dscfm/MMBtu @ %O2 9190 9190 0 6,126.667

Round Duct Diameter, inches 0 0 0

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10320 10320 0 6,880.000

Fc 1420 1420 0 946.667

Monday, March 07, 2011 Page 11 of 13
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

Monday, March 07, 2011 Page 12 of 13
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

Monday, March 07, 2011 Page 13 of 13