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, February 07, 2011 Page 1 of 19
Facility Information:

Plant Scherer

10986 Highway 87

Juliette Ga 31046

Contact: Sarah Markham

Phone: 205-257-6780

Fax:

Email: sasander@southernco.com

Testing Company:

Weston Solutions

1625 Pumphrey Ave

Auburn Al 36832

Contact:Jon Howard

Phone: 334-466-5600

Fax: 334-466-5660

Email: Jon.Howard@westonsolutions.com

Air Permit Number: Permitted Source ID/Name:

3

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

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 324 0 0 0 8148 3852 4 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack % H2O Method 1 - 4 3 0

Stack Flowrate Method 1 - 4 3 0

Stack Carbon Monoxide Method 10 3 0

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

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

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

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

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

Monday, February 07, 2011 Page 2 of 19
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.

-This unit was not tested for Formaldehyde and was unnecessarily tested for VOST and Semi-VOST compounds. 

This was a result of the Weston and Southern Company interpretation of the Section 114 Letter and EPA’s lack of 

clarification until after the testing was completed. The data have been included based on discussions with EPA 

personnel.

-It is theorized that issues associated with the Speciated VOST analysis were due to high native source 

concentrations of Sulfur Dioxide (SO2). Specific issues are listed in the “General Comments” section of the 

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

Stack OCDD Method 23 3 0

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

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

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

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

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

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

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

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

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

Stack OCDF Method 23 3 0

Stack Other TCDD Method 23 0

Stack Other PeCDD Method 23 0

Stack Other HxCDD Method 23 0

Stack Other HpCDD Method 23 0

Stack Other TCDF Method 23 0

Stack Other PeCDF Method 23 0

Stack Other HxCDF Method 23 0

Stack Other HpCDF Method 23 0

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

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

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

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

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

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

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

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

HxCB (PCBs156/157)

Stack Method 23 3 0

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

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

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

(PCB189)

Stack Method 23 3 0

Stack Total PCBs Method 23 3 0

Total organic compounds 

(TOC) as Propane

Stack Method 25A 3 0

Stack Co2 Method 3A CO2 3 0

Stack O2 Method 3A O2 3 0

Monday, February 07, 2011 Page 3 of 19
Maxxam Analytics test report, Appendix D of the attached test report. Also, because of this effect several 

compounds, including chloromethane, were affected and should be considered estimated values.

Maxxam Analytics comments:

-The samples (VOST) exhibited extremely high levels of non-target compounds, mainly siloxanes, based on 

standards calibration criteria and response factors within the GC/MS, which caused the following to occur within the 

analytical sequence(s).

a)	The last internal standard (Bromofluorobenzene) failed for many of the samples

b)	Following completion of an analytical run, we were unable to rid the system of these non-target analytes, thus 

inducing possible carryover into the subsequent analytical run(s).

c)	We dismantled the desorber, rinsed, and baked it in a lab oven. Subsequent reinstallation of the hardware proved 

that residual amounts of the non-target analyte remained.

d)	Repeated step c) again and finally were able to get to “clean” and ready.

e)	Often difficult to meet the tuning criteria for the method and experienced huge losses of sensitivity on the system 

up to 2/3 of standard sensitivity.

f)	Often could not get continuing calibrations to pass after running samples and it took hours of running calibrations 

to get the system to pass the continuing calibration criteria.

- Speciated VOST runs 1-3: levels of MeCl2 and other select target compounds were found in the sample tube blank 

and solvent blank. The run to run data appears to be related to a level of contamination.

-Speciated VOST tube pairs were evaluated separately for inter-run variability and the average of the selected tube 

pairs was used to for reporting purposes. This reporting procedure does not differ significantly from a total mass and 

total sample volume procedure.

-Semi-VOST runs 1-3: Bis (2-ethylheyl) phthalate, this compound is commonly found in plastics, it is not a common 

combustion product but an artifact of sample recovery or lab handling.

-Method 25A (THC)- Due to the very low levels found in the source gas a response time study would not be 

representative as written in the methods. 

-Method 25A -The span gas values (low and mid) were not between method specified limits for percentage of 

achieved span concentration. Low span achieved 20%, method limits 25-35%. Mid span achieved 41%, method 

limits 45-55%.

-Method 25A -The test report and ERT have different values. The test report uses the approach set forth in the 

method, whereas, the ERT contains actual analyzer results. These results presented in the ERT contain values that 

show analyzer drift and include values below zero.

- Method 18 (Methane): Due to low methane concentrations in the source sample, a bag stability study was 

performed in lieu of a recovery study. Subsequently, the data presented in the test report have not been corrected for 

the 70-130% spike recovery procedure.

-Method 18 - the instrument response for each injection was not within 5% of mean response for the instrument.

-Method 18 - A mid range calibration standard wasn't analyzed after all samples were run.

Monday, February 07, 2011 Page 4 of 19
Monday, February 07, 2011 Page 5 of 19
Sampling / Stack Data Results Summary

Location Stack - 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

Location Stack - Method 23

Average

Run Number 2 3 4

Test Date 1/13/2010 1/13/2010 1/14/2010

Run Start Time 6:17:00 AM 1:16:00 PM 6:31:00 AM

Run Finish Time 2:54:00 PM 9:44:00 PM 3:29:00 PM

Net Run Time, minutes 480 480 480

Dry Gas Meter Volume Sampled, dscf 317.562 288.373 306.980 304.305

Moisture Content of Stack Gas, % 11.03 11.75 11.56 11.447

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

Carbon Dioxide, % 14.1 14.4 14 14.167

Oxygen, % 5.7 5.5 5.8 5.667

Average Stack Gas Temperature, °F 273.85 282.41 269.54 275.267

Dry Volumetric Flow Rate, dry scfm 1,942,876.5 1,832,575.7 1,876,164.1 1,883,872.10

0

Actual Wet Volumetric Flue Gas Flow Rate, acfm 3,129,242.1 3,010,379.7 3,023,090.4 3,054,237.40

0

Percent Isokinetic of Sampling Rate, % 100.1 100.6 100.2 100.300

F-Factor, dscfm/MMBtu @ %O2 9820 9820 9820 9,820.000

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Monday, February 07, 2011 Page 6 of 19
Location Stack - 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

Location Stack - 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

Monday, February 07, 2011 Page 7 of 19
Location Stack - 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

Monday, February 07, 2011 Page 8 of 19
Emissions Summary

Location: Stack - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 1.60E-01 9.65E-02 9.59E-02 0.117

ppm 1.66E+02 9.89E+01 9.71E+01 120.667

ppm@7%O2 1.49E+02 8.99E+01 8.94E+01 109.433

Location: Stack - Method 23

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

Average

RunNumber 2 3 4

Mass_mg 0.0000000028 0.0000000091 0.0000000022 0.000

lb/mmBtuO2 2.62E-13 9.27E-13 2.15E-13 0.000

ng/dscm 3.11E-04 1.11E-03 2.53E-04 0.001

ng/dscm@7%O2 2.84E-04 1.00E-03 2.33E-04 0.001

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

Average

RunNumber 2 3 4

Mass_mg 0.0000000014 0.000000008 0.0000000014 0.000

lb/mmBtuO2 1.31E-13 8.15E-13 1.37E-13 0.000

ng/dscm 1.56E-04 9.80E-04 1.61E-04 0.000

ng/dscm@7%O2 1.43E-04 8.85E-04 1.48E-04 0.000

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

Average

RunNumber 2 3 4

Mass_mg 0.0000000017 0.0000000019 0.0000000018 0.000

lb/mmBtuO2 1.59E-13 1.94E-13 1.76E-13 0.000

ng/dscm 1.89E-04 2.33E-04 2.07E-04 0.000

ng/dscm@7%O2 1.73E-04 2.10E-04 1.91E-04 0.000

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

Average

RunNumber 2 3 4

Mass_mg 0.0000000018 0.0000000018 0.0000000018 0.000

lb/mmBtuO2 1.69E-13 1.83E-13 1.76E-13 0.000

ng/dscm 2.00E-04 2.20E-04 2.07E-04 0.000

ng/dscm@7%O2 1.83E-04 1.99E-04 1.91E-04 0.000

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

Average

RunNumber 2 3 4

Mass_mg 0.0000000016 0.0000000071 0.0000000016 0.000

lb/mmBtuO2 1.50E-13 7.23E-13 1.56E-13 0.000

ng/dscm 1.78E-04 8.70E-04 1.84E-04 0.000

ng/dscm@7%O2 1.63E-04 7.85E-04 1.69E-04 0.000

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

Average

Monday, February 07, 2011 Page 9 of 19
RunNumber 2 3 4

Mass_mg 0.0000000017 0.000000002 0.0000000017 0.000

lb/mmBtuO2 1.59E-13 2.04E-13 1.66E-13 0.000

ng/dscm 1.89E-04 2.45E-04 1.96E-04 0.000

ng/dscm@7%O2 1.73E-04 2.21E-04 1.80E-04 0.000

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

Average

RunNumber 2 3 4

Mass_mg 0.0000000014 0.0000000028 0.0000000014 0.000

lb/mmBtuO2 1.31E-13 2.85E-13 1.37E-13 0.000

ng/dscm 1.56E-04 3.43E-04 1.61E-04 0.000

ng/dscm@7%O2 1.43E-04 3.10E-04 1.48E-04 0.000

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

Average

RunNumber 2 3 4

Mass_mg 0.0000000016 0.0000000016 0.0000000016 0.000

lb/mmBtuO2 1.50E-13 1.63E-13 1.56E-13 0.000

ng/dscm 1.78E-04 1.96E-04 1.84E-04 0.000

ng/dscm@7%O2 1.63E-04 1.77E-04 1.69E-04 0.000

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

Average

RunNumber 2 3 4

Mass_mg 0.0000000018 0.0000000021 0.0000000018 0.000

lb/mmBtuO2 1.69E-13 2.14E-13 1.76E-13 0.000

ng/dscm 2.00E-04 2.57E-04 2.07E-04 0.000

ng/dscm@7%O2 1.83E-04 2.32E-04 1.91E-04 0.000

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

Average

RunNumber 2 3 4

Mass_mg 0.0000000017 0.0000000015 0.0000000015 0.000

lb/mmBtuO2 1.59E-13 1.53E-13 1.46E-13 0.000

ng/dscm 1.89E-04 1.84E-04 1.73E-04 0.000

ng/dscm@7%O2 1.73E-04 1.66E-04 1.59E-04 0.000

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

Average

RunNumber 2 3 4

Mass_mg 0.000000002 0.000000003 0.0000000018 0.000

lb/mmBtuO2 1.87E-13 3.06E-13 1.76E-13 0.000

ng/dscm 2.22E-04 3.67E-04 2.07E-04 0.000

ng/dscm@7%O2 2.03E-04 3.31E-04 1.91E-04 0.000

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

Average

RunNumber 2 3 4

Mass_mg 0.000000013 0.000000017 0.000000014 0.000

lb/mmBtuO2 1.22E-12 1.73E-12 1.37E-12 0.000

ng/dscm 1.45E-03 2.08E-03 1.61E-03 0.002

ng/dscm@7%O2 1.33E-03 1.88E-03 1.48E-03 0.002

Monday, February 07, 2011 Page 10 of 19
Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC

Average

RunNumber 2 3 4

Mass_mg 0.0000000088 0.000000041 0.000000015 0.000

lb/mmBtuO2 8.25E-13 4.18E-12 1.46E-12 0.000

ng/dscm 9.79E-04 5.02E-03 1.73E-03 0.003

ng/dscm@7%O2 8.95E-04 4.53E-03 1.59E-03 0.002

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

Average

RunNumber 2 3 4

Mass_mg 0.000000041 0.000000066 0.000000013 0.000

lb/mmBtuO2 3.84E-12 6.72E-12 1.27E-12 0.000

ng/dscm 4.56E-03 8.08E-03 1.50E-03 0.005

ng/dscm@7%O2 4.17E-03 7.29E-03 1.38E-03 0.004

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

Average

RunNumber 2 3 4

Mass_mg 0.0000000087 0.000000019 0.000000011 0.000

lb/mmBtuO2 8.16E-13 1.94E-12 1.07E-12 0.000

ng/dscm 9.68E-04 2.33E-03 1.27E-03 0.002

ng/dscm@7%O2 8.85E-04 2.10E-03 1.17E-03 0.001

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

Average

RunNumber 2 3 4

Mass_mg 0.000000008 0.000000011 0.00000001 0.000

lb/mmBtuO2 7.50E-13 1.12E-12 9.76E-13 0.000

ng/dscm 8.90E-04 1.35E-03 1.15E-03 0.001

ng/dscm@7%O2 8.14E-04 1.22E-03 1.06E-03 0.001

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

Average

RunNumber 2 3 4

Mass_mg 0.00000014 0.00000018 0.000000077 0.000

lb/mmBtuO2 1.31E-11 1.83E-11 7.52E-12 0.000

ng/dscm 1.56E-02 2.20E-02 8.86E-03 0.015

ng/dscm@7%O2 1.43E-02 1.99E-02 8.16E-03 0.014

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

Average

RunNumber 2 3 4

Mass_mg 0.0000000081 0.000000011 0.00000001 0.000

lb/mmBtuO2 7.59E-13 1.12E-12 9.76E-13 0.000

ng/dscm 9.01E-04 1.35E-03 1.15E-03 0.001

ng/dscm@7%O2 8.24E-04 1.22E-03 1.06E-03 0.001

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

Average

RunNumber 2 3 4

Mass_mg 0.0000000018 0.0000000048 0.0000000026 0.000

lb/mmBtuO2 1.69E-13 4.89E-13 2.54E-13 0.000

Monday, February 07, 2011 Page 11 of 19
ng/dscm 2.00E-04 5.88E-04 2.99E-04 0.000

ng/dscm@7%O2 1.83E-04 5.31E-04 2.75E-04 0.000

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

Average

RunNumber 2 3 4

Mass_mg 0.0000000019 0.0000000053 0.0000000042 0.000

lb/mmBtuO2 1.78E-13 5.40E-13 4.10E-13 0.000

ng/dscm 2.11E-04 6.49E-04 4.83E-04 0.000

ng/dscm@7%O2 1.93E-04 5.86E-04 4.45E-04 0.000

Compound: 2,3,7,8-TCDD

Average

RunNumber 2 3 4

Mass_mg 0.0000000019 0.0000000015 0.0000000015 0.000

lb/mmBtuO2 1.78E-13 1.53E-13 1.46E-13 0.000

ng/dscm 2.11E-04 1.84E-04 1.73E-04 0.000

ng/dscm@7%O2 1.93E-04 1.66E-04 1.59E-04 0.000

Compound: 2,3,7,8-TCDF

Average

RunNumber 2 3 4

Mass_mg 0.0000000028 0.0000000074 0.0000000059 0.000

lb/mmBtuO2 2.62E-13 7.54E-13 5.76E-13 0.000

ng/dscm 3.11E-04 9.06E-04 6.79E-04 0.001

ng/dscm@7%O2 2.84E-04 8.18E-04 6.25E-04 0.001

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

Average

RunNumber 2 3 4

Mass_mg 0.000000009 0.000000019 0.000000011 0.000

lb/mmBtuO2 8.44E-13 1.94E-12 1.07E-12 0.000

ng/dscm 1.00E-03 2.33E-03 1.27E-03 0.002

ng/dscm@7%O2 9.14E-04 2.10E-03 1.17E-03 0.001

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

Average

RunNumber 2 3 4

Mass_mg 0.0000000079 0.000000011 0.00000001 0.000

lb/mmBtuO2 7.41E-13 1.12E-12 9.76E-13 0.000

ng/dscm 8.79E-04 1.35E-03 1.15E-03 0.001

ng/dscm@7%O2 8.04E-04 1.22E-03 1.06E-03 0.001

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

Average

RunNumber 2 3 4

Mass_mg 0.00000002 0.000000053 0.000000015 0.000

lb/mmBtuO2 1.87E-12 5.40E-12 1.46E-12 0.000

ng/dscm 2.22E-03 6.49E-03 1.73E-03 0.003

ng/dscm@7%O2 2.03E-03 5.86E-03 1.59E-03 0.003

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

Average

RunNumber 2 3 4

Monday, February 07, 2011 Page 12 of 19
Mass_mg 0.000000014 0.00000002 0.000000011 0.000

lb/mmBtuO2 1.31E-12 2.04E-12 1.07E-12 0.000

ng/dscm 1.56E-03 2.45E-03 1.27E-03 0.002

ng/dscm@7%O2 1.43E-03 2.21E-03 1.17E-03 0.002

Compound: OCDD

Average

RunNumber 2 3 4

Mass_mg 0.0000000101 0.0000000246 0.0000000073 0.000

lb/mmBtuO2 9.47E-13 2.51E-12 7.13E-13 0.000

ng/dscm 1.12E-03 3.01E-03 8.40E-04 0.002

ng/dscm@7%O2 1.02E-03 2.72E-03 7.73E-04 0.002

Compound: OCDF

Average

RunNumber 2 3 4

Mass_mg 0.0000000043 0.0000000059 0.0000000035 0.000

lb/mmBtuO2 4.03E-13 6.01E-13 3.42E-13 0.000

ng/dscm 4.78E-04 7.23E-04 4.03E-04 0.001

ng/dscm@7%O2 4.37E-04 6.53E-04 3.71E-04 0.000

Compound: Other HpCDD

Average

RunNumber 2 3 4

Mass_mg 0.0000000018 0.0000000057 0 0.000

lb/mmBtuO2 1.69E-13 5.81E-13 0.00E+00 0.000

ng/dscm 2.00E-04 6.98E-04 0.00E+00 0.000

ng/dscm@7%O2 1.83E-04 6.30E-04 0.00E+00 0.000

Compound: Other HpCDF

Average

RunNumber 2 3 4

Mass_mg 0 0 0 0.000

lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Other HxCDD

Average

RunNumber 2 3 4

Mass_mg 0 0.000000003 0 0.000

lb/mmBtuO2 0.00E+00 3.06E-13 0.00E+00 0.000

ng/dscm 0.00E+00 3.67E-04 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 3.31E-04 0.00E+00 0.000

Compound: Other HxCDF

Average

RunNumber 2 3 4

Mass_mg 0 0.0000000038 0 0.000

lb/mmBtuO2 0.00E+00 3.87E-13 0.00E+00 0.000

ng/dscm 0.00E+00 4.65E-04 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 4.20E-04 0.00E+00 0.000

Monday, February 07, 2011 Page 13 of 19
Process Run Data

Compound: Other PeCDD

Average

RunNumber 2 3 4

Mass_mg 0 0 0 0.000

lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Other PeCDF

Average

RunNumber 2 3 4

Mass_mg 0 0 0.0000000046 0.000

lb/mmBtuO2 0.00E+00 0.00E+00 4.49E-13 0.000

ng/dscm 0.00E+00 0.00E+00 5.29E-04 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 4.87E-04 0.000

Compound: Other TCDD

Average

RunNumber 2 3 4

Mass_mg 0 0.0000000396 0.0000000003 0.000

lb/mmBtuO2 0.00E+00 4.03E-12 2.93E-14 0.000

ng/dscm 0.00E+00 4.85E-03 3.45E-05 0.002

ng/dscm@7%O2 0.00E+00 4.38E-03 3.18E-05 0.001

Compound: Other TCDF

Average

RunNumber 2 3 4

Mass_mg 0 0.0000000023 0.0000000056 0.000

lb/mmBtuO2 0.00E+00 2.34E-13 5.47E-13 0.000

ng/dscm 0.00E+00 2.82E-04 6.44E-04 0.000

ng/dscm@7%O2 0.00E+00 2.55E-04 5.93E-04 0.000

Compound: Total PCBs

Average

RunNumber 2 3 4

Mass_mg 0.000017 0.000019 0.0000046 0.000

lb/mmBtuO2 1.59E-09 1.94E-09 4.49E-10 0.000

ng/dscm 1.89E+00 2.33E+00 5.29E-01 1.583

ng/dscm@7%O2 1.73E+00 2.10E+00 4.87E-01 1.439

Location: Stack - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 9.24E-04 9.52E-04 9.65E-04 0.001

ppm 6.10E-01 6.20E-01 6.20E-01 0.617

ppm@7%O2 5.47E-01 5.63E-01 5.71E-01 0.560

Monday, February 07, 2011 Page 14 of 19
Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Gross Electric Output 879.93 MW 0

2 Gross Electric Output 880.05 MW 0

3 Gross Electric Output 880.14 MW 0

4 Gross Electric Output 0 MW 0

5 Gross Electric Output 0 MW 0

Run Name Value UOM Comments

1 Coal Fuel Analysis 8661

2 Coal Fuel Analysis 8573

3 Coal Fuel Analysis 8721

4 Coal Fuel Analysis 8566

5 Coal Fuel Analysis 8553

6 Coal Fuel Analysis 8568

Monday, February 07, 2011 Page 15 of 19
Sampling / Stack Data Results Detail

Location Stack - 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

Monday, February 07, 2011 Page 16 of 19
Location Stack - Method 23

Average

Run Number 2 3 4

Test Date 1/13/2010 1/13/2010 1/14/2010

Run Start Time 6:17:00 AM 1:16:00 PM 6:31:00 AM

Run Finish Time 2:54:00 PM 9:44:00 PM 3:29:00 PM

Net Traversing Points 96 96 96

Net Run Time, minutes 480 480 480

Nozzle Diameter, inches 0.189 0.185 0.189 0.188

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.972 0.978 0.972 0.974

Barometric Pressure, inches of Mercury 29.3 29.3 29.25 29.283

Average Orifice Meter Differential, inches H2O 1.53 1.25 1.46 1.413

Dry Gas Meter Volume Sampled, cubic feet 331.749 305.541 324.223 320.504

Average Dry Gas Meter Temperature, °F 67.05 77.47 71.85 72.123

Dry Gas Meter Volume Sampled, dscf 317.562 288.373 306.980 304.305

Total Moisture Liquid collected, g 836.7 816.1 852.0999999

99999

834.967

Volume of Water Vapor, standard cubic feet 39.38 38.41 40.11 39.300

Moisture Content of Stack Gas, % 11.03 11.75 11.56 11.447

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

Dry Mole Fraction 0.8897 0.8825 0.8844 0.886

Carbon Dioxide, % 14.1 14.4 14 14.167

Oxygen, % 5.7 5.5 5.8 5.667

Carbon Monoxide & Nitrogen, % 80.2 80.1 80.2 80.167

Fuel Factor 1.08 1.07 1.08

Dry Molecular Weight, lb/lb-Mole 30.48 30.52 30.47 30.490

Wet Molecular weight, lb/lb-Mole 29.10 29.05 29.03 29.060

Flue Gas Static Pressure, inches of H2O -3.8 -3.8 -3.2 -3.600

Absolute Flue Gas Pressure, inches of Mercury 29.02 29.02 29.01 29.017

Average Stack Gas Temperature, °F 273.85 282.41 269.54 275.267

Average Velocity Head, inches of H2O 1.8515090521

9117

1.690861465

64455

1.733514653

91745

1.759

Average Stack Gas Velocity, feet/second 91.09 87.63 88.00 88.907

Stack Cross-Sectional Area, square feet 572.555 572.555 572.555 572.555

Dry Volumetric Flow Rate, dry scfm 1,942,876.5 1,832,575.7 1,876,164.1 1,883,872.1

00

Actual Wet Volumetric Flue Gas Flow Rate, acfm 3,129,242.1 3,010,379.7 3,023,090.4 3,054,237.4

00

Percent Isokinetic of Sampling Rate, % 100.1 100.6 100.2 100.300

Percent Excess Air, % 36.8 35.2 37.7 36.567

F-Factor, dscfm/MMBtu @ %O2 9820 9820 9820 9,820.000

Round Duct Diameter, inches 324 324 324

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

Monday, February 07, 2011 Page 17 of 19
Location Stack - 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

Monday, February 07, 2011 Page 18 of 19
Location Stack - 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

Monday, February 07, 2011 Page 19 of 19
Location Stack - 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

Monday, February 07, 2011 Page 20 of 19