Name:

Title:

Company:

Sign Date:

Name: Joshep Oven, PE

Title: Senior Project Manager

Company: Weston Solutions, Inc.

Sign Date: 9/22/2010

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.

Monday, January 31, 2011 Page 1 of 14
Facility Information:

OUC-Stanton Energy Center

5100 South Alafaya Trail

Orlando Fl 32831

Contact: David Baez

Phone:

Fax:

Email:

Testing Company:

Weston Solutions

1625 Pumphrey Ave

Auburn Al 36832

Contact:Joe Oven

Phone: 334-466-5600

Fax:

Email: Joe.Oven@WestonSolutions.com

Air Permit Number:

564

Permitted Source ID/Name:

2 Stanton Energy Center Unit 2

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

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

 process flow diagram:

See attached report

Industry/SCC/NAIS

Sampling Location Information:

Test Parameter Information:

AFS #: FRS #:

SCC / Description

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

Location

Round

Duct

Diam.

Distance from 

upstream dist.

Distance from

downstream dist.

Number of

Traverse Ports

Equiv. 

Diam

Min.Travers 

Points

Rect. Duct 

Length /Width

Stack 247.44 0 0 0 165 240 4 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Carbon Monoxide Method 10 3 0

Total organic compounds 

(TOC) as Propane

Stack Method 25A 3 0

Stack Hydrogen Chloride Method 26A 3 0

Stack Hydrogen Fluoride Method 26A 3 0

Stack Total Particulate OTM - 28 3 0

Organic Condensible 

Particulate

Stack OTM - 28 3 0

Monday, January 31, 2011 Page 2 of 14
The following describes any modifications and/or deviations to the applicable test 

methods. If alternative methods were requested, see the attachments for documentation 

of request AND approval, including dates.

See attached report

Inorganic (Aqueous) 

Condensible Part.

Stack OTM - 28 3 0

Stack Cadmium Method 29 3 0

Stack Arsenic Method 29 3 0

Stack Antimony Method 29 3 0

Stack Manganese Method 29 3 0

Stack Lead Method 29 3 0

Stack Cobalt Method 29 3 0

Stack Beryllium Method 29 3 0

Stack Selenium Method 29 3 0

Stack Nickel Method 29 3 0

Stack Phosphorus (yellow or white) Method 29 3 0

Stack Filterable Particulate Method 29 3 0

Stack Chromium Method 29 3 0

Stack O2 Method 3A O2 3 0

Stack Co2 Method 3A CO2 3 0

Stack Filterable Particulate Method 5 3 0

Monday, January 31, 2011 Page 3 of 14
Sampling / Stack Data Results Summary

Location Stack - Method 26A

Average

Run Number 1 2 3

Test Date 6/23/2010 6/23/2010 6/23/2010

Run Start Time 8:19:00 AM 9:48:00 

AM

11:10:00 AM

Run Finish Time 9:32:00 AM 11:01:00 

AM

1:55:00 PM

Net Run Time, minutes 60 60 60

Dry Gas Meter Volume Sampled, dscf 34.470 35.141 34.957 34.856

Moisture Content of Stack Gas, % 34.42 34.33 20.11 29.620

Moisture Saturation at Stack Gas Temperature, % 14.04 13.91 13.98 13.977

Carbon Dioxide, % 12.7 12.7 15.9 13.767

Oxygen, % 6.6 6.6 7.5 6.900

Average Stack Gas Temperature, °F 126.83 126.50 126.67 126.667

Dry Volumetric Flow Rate, dry scfm 931,775.3 942,773.3 977,888.8 950,812.467

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,219,411.7 1,230,832.4 1,278,518.9 1,242,921.00

0

Percent Isokinetic of Sampling Rate, % 109.1 109.9 105.4 108.133

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

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Monday, January 31, 2011 Page 4 of 14
Location Stack - 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 - Method 5

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, January 31, 2011 Page 5 of 14
Location Stack - OTM - 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, January 31, 2011 Page 6 of 14
Emissions Summary

Location: Stack - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 1.7 0.969 0.754 1.141

lb/mmBtuO2 1.55E-03 8.69E-04 7.25E-04 0.001

ppm 1.15E+00 6.42E-01 5.03E-01 0.765

ppm@7%O2 1.12E+00 6.24E-01 5.22E-01 0.755

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.097 0.088 0.09 0.092

lb/mmBtuO2 8.87E-05 7.89E-05 8.66E-05 0.000

ppm 1.19E-01 1.06E-01 1.09E-01 0.111

ppm@7%O2 1.16E-01 1.03E-01 1.13E-01 0.111

Location: Stack - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.0018 0.0018 0.0018 0.002

Elb/hr 1.60E-03 1.61E-03 1.61E-03 0.002

lb/mmBtuO2 3.89E-07 3.83E-07 3.80E-07 0.000

mg/dscm 4.37E-04 4.26E-04 4.26E-04 0.000

mg/dscm@7%O2 4.25E-04 4.17E-04 4.14E-04 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.0018 0.0018 0.0018 0.002

Elb/hr 1.60E-03 1.61E-03 1.61E-03 0.002

lb/mmBtuO2 3.89E-07 3.83E-07 3.80E-07 0.000

mg/dscm 4.37E-04 4.26E-04 4.26E-04 0.000

mg/dscm@7%O2 4.25E-04 4.17E-04 4.14E-04 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.00045 0.00045 0.00045 0.000

Elb/hr 4.00E-04 4.04E-04 4.03E-04 0.000

lb/mmBtuO2 9.74E-08 9.58E-08 9.51E-08 0.000

mg/dscm 1.09E-04 1.07E-04 1.07E-04 0.000

mg/dscm@7%O2 1.06E-04 1.05E-04 1.04E-04 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.00051 0.00045 0.00045 0.000

Elb/hr 4.53E-04 4.04E-04 4.03E-04 0.000

lb/mmBtuO2 1.10E-07 9.58E-08 9.51E-08 0.000

Monday, January 31, 2011 Page 7 of 14
mg/dscm 1.24E-04 1.07E-04 1.07E-04 0.000

mg/dscm@7%O2 1.21E-04 1.05E-04 1.04E-04 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.0067 0.01183 0.00473 0.008

Elb/hr 5.95E-03 1.06E-02 4.24E-03 0.007

lb/mmBtuO2 1.45E-06 2.52E-06 9.99E-07 0.000

mg/dscm 1.62E-03 2.80E-03 1.12E-03 0.002

mg/dscm@7%O2 1.57E-03 2.74E-03 1.09E-03 0.002

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.02095 0.00073 0.00062 0.007

Elb/hr 1.86E-02 6.55E-04 5.55E-04 0.007

lb/mmBtuO2 4.53E-06 1.55E-07 1.31E-07 0.000

mg/dscm 5.08E-03 1.73E-04 1.47E-04 0.002

mg/dscm@7%O2 4.94E-03 1.69E-04 1.43E-04 0.002

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 182 63 68 104.333

Elb/hr 1.62E+02 5.65E+01 6.09E+01 93.133

lb/mmBtuO2 3.94E-02 1.34E-02 1.44E-02 0.022

mg/dscm 4.41E+01 1.49E+01 1.61E+01 25.033

mg/dscm@7%O2 4.29E+01 1.46E+01 1.56E+01 24.367

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.00262 0.00134 0.0009 0.002

Elb/hr 2.33E-03 1.20E-03 8.06E-04 0.001

lb/mmBtuO2 5.67E-07 2.85E-07 1.90E-07 0.000

mg/dscm 6.35E-04 3.17E-04 2.13E-04 0.000

mg/dscm@7%O2 6.17E-04 3.10E-04 2.07E-04 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.031 0.0215 0.0139 0.022

Elb/hr 2.75E-02 1.93E-02 1.25E-02 0.020

lb/mmBtuO2 6.71E-06 4.57E-06 2.94E-06 0.000

mg/dscm 7.52E-03 5.09E-03 3.29E-03 0.005

mg/dscm@7%O2 7.31E-03 4.98E-03 3.20E-03 0.005

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.00464 0.07564 0.00314 0.028

Elb/hr 4.12E-03 6.79E-02 2.81E-03 0.025

lb/mmBtuO2 1.00E-06 1.61E-05 6.63E-07 0.000

Monday, January 31, 2011 Page 8 of 14
Process Run Data

mg/dscm 1.13E-03 1.79E-02 7.43E-04 0.007

mg/dscm@7%O2 1.10E-03 1.75E-02 7.22E-04 0.006

Compound: Phosphorus (yellow or white)

Average

RunNumber 1 2 3

Mass_mg 0.0509 0.05565 0.05945 0.055

Elb/hr 4.52E-02 4.99E-02 5.33E-02 0.049

lb/mmBtuO2 1.10E-05 1.18E-05 1.26E-05 0.000

mg/dscm 1.23E-02 1.32E-02 1.41E-02 0.013

mg/dscm@7%O2 1.20E-02 1.29E-02 1.37E-02 0.013

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.1358 0.1256 0.1501 0.137

Elb/hr 1.21E-01 1.13E-01 1.34E-01 0.123

lb/mmBtuO2 2.94E-05 2.67E-05 3.17E-05 0.000

mg/dscm 3.29E-02 2.97E-02 3.55E-02 0.033

mg/dscm@7%O2 3.20E-02 2.91E-02 3.45E-02 0.032

Location: Stack - Method 5

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 182 63 68 104.333

lb/mmBtuO2 4.32E-02 1.46E-02 1.58E-02 0.025

Location: Stack - OTM - 28

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 14 5 7 8.667

lb/mmBtuO2 3.32E-03 1.16E-03 1.62E-03 0.002

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 1 1 1 1.000

lb/mmBtuO2 2.37E-04 2.32E-04 2.32E-04 0.000

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 15 6 8 9.667

lb/mmBtuO2 3.56E-03 1.39E-03 1.86E-03 0.002

Monday, January 31, 2011 Page 9 of 14
Process Run Data

APCD Run Data

Process Lab Run Data

Monday, January 31, 2011 Page 10 of 14
Sampling / Stack Data Results Detail

Location Stack - Method 26A

Average

Run Number 1 2 3

Test Date 6/23/2010 6/23/2010 6/23/2010

Run Start Time 8:19:00 AM 9:48:00 AM 11:10:00 AM

Run Finish Time 9:32:00 AM 11:01:00 AM 1:55:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 60 60 60

Nozzle Diameter, inches 0.186 0.186 0.186 0.186

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.986 0.986 0.986 0.986

Barometric Pressure, inches of Mercury 29.57 29.57 29.57 29.570

Average Orifice Meter Differential, inches H2O 1.17 1.20 1.21 1.193

Dry Gas Meter Volume Sampled, cubic feet 36.762 37.782 37.679 37.408

Average Dry Gas Meter Temperature, °F 90.33 94.83 96.25 93.803

Dry Gas Meter Volume Sampled, dscf 34.470 35.141 34.957 34.856

Total Moisture Liquid collected, g 384.3 390.2 187 320.500

Volume of Water Vapor, standard cubic feet 18.09 18.37 8.80 15.087

Moisture Content of Stack Gas, % 34.42 34.33 20.11 29.620

Moisture Saturation at Stack Gas Temperature, % 14.04 13.91 13.98 13.977

Dry Mole Fraction 0.8596 0.8609 0.8602 0.860

Carbon Dioxide, % 12.7 12.7 15.9 13.767

Oxygen, % 6.6 6.6 7.5 6.900

Carbon Monoxide & Nitrogen, % 80.7 80.7 76.6 79.333

Fuel Factor 1.13 1.13 0.84

Dry Molecular Weight, lb/lb-Mole 30.30 30.30 30.84 30.480

Wet Molecular weight, lb/lb-Mole 32.24 32.26 30.15 31.550

Flue Gas Static Pressure, inches of H2O -0.07 -0.06 -0.07 -0.067

Absolute Flue Gas Pressure, inches of Mercury 29.56 29.57 29.56 29.563

Average Stack Gas Temperature, °F 126.83 126.50 126.67 126.667

Average Velocity Head, inches of H2O 1.1666004781

3367

1.190022525

4633

1.199341106

38725

1.185

Average Stack Gas Velocity, feet/second 60.86 61.43 63.81 62.033

Stack Cross-Sectional Area, square feet 333.939 333.939 333.939 333.939

Dry Volumetric Flow Rate, dry scfm 931,775.3 942,773.3 977,888.8 950,812.467

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,219,411.7 1,230,832.4 1,278,518.9 1,242,921.0

00

Percent Isokinetic of Sampling Rate, % 109.1 109.9 105.4 108.133

Percent Excess Air, % 44.9 44.9 59.0 49.600

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

Round Duct Diameter, inches 247.44 247.44 247.44

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Monday, January 31, 2011 Page 11 of 14
Location Stack - 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, January 31, 2011 Page 12 of 14
Location Stack - Method 5

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, January 31, 2011 Page 13 of 14
Location Stack - OTM - 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, January 31, 2011 Page 14 of 14