### 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 24

### Facility Information:

San Juan 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: Enter the Boiler ID of the tested boiler (left) SJ7 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/NAIS221112

Sampling Location Information:

Test Parameter Information: AFS #:Enter ARS ID FRS #:Enter FRS ID

SCC / Description10100202 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous Coal - Pulverized Coal: Dry Bottom (Bituminous Coal)

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

Location Round

Duct Diam. Distance from upstream dist. Distance from

downstream dist. Number of

Traverse Ports Equiv. Diam Min.Travers Points Rect. Duct Length /Width Stack Exit 0 0 0 0 0 0 0 0

Target Parameter Test Method Number of

Test RunsTest Run

DurationSample

Points Comments Location% 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 Stack Exit



### Monday, March 07, 2011 Page 2 of 241,2,3,7,8,9-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 Stack Exit 2,3,3',4,4',5/2,3,3',4,4',5'-

HxCB (PCBs156/157) 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 Stack Exit 2,3,3',4,4',5,5'-HpCB

(PCB189) Method 23 3 480 0 Stack Exit

Total PCBs Method 23 3 480 0 Stack Exit Total TEQ Method 23 3 480 0 Stack Exit Total organic compounds

(TOC) as Propane 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 Stack Exit 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 24

### 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

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 Stack Exit 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

Filterable Particulate Method 5 3 240 0 Stack Exit Filterable Particulate Method 5/OTM-28 3 240 0 Use only for wet stacks. Delete OTM27/OTM28 test. Stack Exit

Sulfur Dioxide Method 6C 3 180 0 Stack Exit Nitrogen oxides (NOx) Method 7E 3 180 0 Stack Exit



### Monday, March 07, 2011 Page 4 of 24

### Sampling / Stack Data Results Summary



### LocationStack Exit - Method 23 Average Run Number 1 2 3 Test Date 10/25/201010/27/2010 10/28/2010 Run Start Time 8:29:00 AM 8:52:00 AM8:29:00 AM

Run Finish Time 4:57:00 PM5:02:00 PM4:57:00 PM Net Run Time, minutes 480 480 480 Dry Gas Meter Volume Sampled, dscf 172.027 170.512 172.027 171.522 Moisture Content of Stack Gas, % 11.20 10.81 11.20 11.070 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 12.8 12.8 12.8 12.800 Oxygen, % 4.9 5 4.9 4.933 Average Stack Gas Temperature, °F 291.08 291.98 291.08 291.380 Dry Volumetric Flow Rate, dry scfm 0.0 0.0 0.0 0.000 Actual Wet Volumetric Flue Gas Flow Rate, acfm 0.0 0.0 0.0 0.000 Percent Isokinetic of Sampling Rate, % 100.4 102.1 100.4 100.967 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000



### Monday, March 07, 2011 Page 5 of 24

### LocationStack Exit - Method 29 Average

Run Number 1 2 3 Test Date 10/26/201010/26/2010 10/27/2010 Run Start Time 8:52:00 AM1:40:00 PM8:49:00 AM Run Finish Time 1:05:00 PM5:53:00 PM1:02:00 PM Net Run Time, minutes 240 240 240 Dry Gas Meter Volume Sampled, dscf 106.595 109.008 105.450 107.018 Moisture Content of Stack Gas, % 11.43 12.27 11.36 11.687 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 13 13.1 13 13.033 Oxygen, % 4.8 4.6 4.6 4.667 Average Stack Gas Temperature, °F 290.17 293.42 290.00 291.197 Dry Volumetric Flow Rate, dry scfm 0.0 0.0 0.0 0.000 Actual Wet Volumetric Flue Gas Flow Rate, acfm 0.0 0.0 0.0 0.000 Percent Isokinetic of Sampling Rate, % 103.1 103.8 101.9 102.933 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000



### LocationStack Exit - OTM - 27/28 Average Run Number 1 2 3 Test Date 10/26/201010/26/2010 10/26/2010 Run Start Time 9:06:00 AM 12:08:00 PM3:49:00 PM

Run Finish Time 11:38:00 AM2:28:00 PM5:57:00 PM Net Run Time, minutes 120 120 120 Dry Gas Meter Volume Sampled, dscf 53.854 45.151 43.336 47.447 Moisture Content of Stack Gas, % 10.02 11.89 11.77 11.227 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 12.7 12.4 12.8 12.633 Oxygen, % 5 5.4 5 5.133 Average Stack Gas Temperature, °F 292.08 294.75 289.75 292.193 Dry Volumetric Flow Rate, dry scfm 0.0 0.0 0.0 0.000 Actual Wet Volumetric Flue Gas Flow Rate, acfm 0.0 0.0 0.0 0.000 Percent Isokinetic of Sampling Rate, % 114.4 98.7 98.8 103.967 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000



### Monday, March 07, 2011 Page 6 of 24

### Emissions Summary



### Location: Stack Exit - Method 23 Compound: 1,2,3,4,6,7,8-HpCDD Average RunNumber 1 2 3 Mass_mg 0.000000002 0.0000000025 0.0000000032 0.000 lb/mmBtuO2 3.08E-13 3.90E-13 4.92E-13 0.000 ng/dscm 4.11E-04 5.18E-04 6.57E-04 0.001 ng/dscm@7%O2 3.57E-04 4.53E-04 5.71E-04 0.000 

### Compound: 1,2,3,4,6,7,8-HpCDF Average RunNumber 1 2 3 Mass_mg 0.0000000015 0.0000000017 0.000000002 0.000 lb/mmBtuO2 2.31E-13 2.66E-13 3.08E-13 0.000 ng/dscm 3.08E-04 3.52E-04 4.11E-04 0.000 ng/dscm@7%O2 2.68E-04 3.08E-04 3.57E-04 0.000 

### Compound: 1,2,3,4,7,8,9-HpCDF Average RunNumber 1 2 3 Mass_mg 0.0000000023 0.0000000025 0.0000000025 0.000 lb/mmBtuO2 3.54E-13 3.90E-13 3.85E-13 0.000 ng/dscm 4.72E-04 5.18E-04 5.13E-04 0.001 ng/dscm@7%O2 4.10E-04 4.53E-04 4.46E-04 0.000 

### Compound: 1,2,3,4,7,8-HxCDD Average RunNumber 1 2 3 Mass_mg 0.000000002 0.0000000018 0.0000000023 0.000 lb/mmBtuO2 3.08E-13 2.81E-13 3.54E-13 0.000 ng/dscm 4.11E-04 3.73E-04 4.72E-04 0.000 ng/dscm@7%O2 3.57E-04 3.26E-04 4.10E-04 0.000 

### Compound: 1,2,3,4,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.0000000013 0.0000000014 0.000000002 0.000 lb/mmBtuO2 2.00E-13 2.19E-13 3.08E-13 0.000 ng/dscm 2.67E-04 2.90E-04 4.11E-04 0.000 ng/dscm@7%O2 2.32E-04 2.54E-04 3.57E-04 0.000 

### Compound: 1,2,3,6,7,8-HxCDD Average RunNumber 1 2 3 Mass_mg 0.0000000021 0.000000002 0.0000000024 0.000 lb/mmBtuO2 3.23E-13 3.12E-13 3.69E-13 0.000 ng/dscm 4.31E-04 4.14E-04 4.93E-04 0.000 ng/dscm@7%O2 3.74E-04 3.62E-04 4.28E-04 0.000 

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



### Monday, March 07, 2011 Page 7 of 24RunNumber 1 2 3 Mass_mg 0.0000000013 0.0000000013 0.0000000018 0.000 lb/mmBtuO2 2.00E-13 2.03E-13 2.77E-13 0.000 ng/dscm 2.67E-04 2.69E-04 3.70E-04 0.000 ng/dscm@7%O2 2.32E-04 2.35E-04 3.21E-04 0.000 

### Compound: 1,2,3,7,8,9-HxCDD Average RunNumber 1 2 3 Mass_mg 0.0000000024 0.000000002 0.0000000025 0.000 lb/mmBtuO2 3.69E-13 3.12E-13 3.85E-13 0.000 ng/dscm 4.93E-04 4.14E-04 5.13E-04 0.000 ng/dscm@7%O2 4.28E-04 3.62E-04 4.46E-04 0.000 

### Compound: 1,2,3,7,8,9-HxCDF Average RunNumber 1 2 3 Mass_mg 0.0000000016 0.0000000018 0.0000000025 0.000 lb/mmBtuO2 2.46E-13 2.81E-13 3.85E-13 0.000 ng/dscm 3.29E-04 3.73E-04 5.13E-04 0.000 ng/dscm@7%O2 2.86E-04 3.26E-04 4.46E-04 0.000 

### Compound: 1,2,3,7,8-PeCDD Average RunNumber 1 2 3 Mass_mg 0.0000000019 0.0000000019 0.0000000026 0.000 lb/mmBtuO2 2.92E-13 2.97E-13 4.00E-13 0.000 ng/dscm 3.90E-04 3.94E-04 5.34E-04 0.000 ng/dscm@7%O2 3.39E-04 3.44E-04 4.64E-04 0.000 

### Compound: 1,2,3,7,8-PeCDF Average RunNumber 1 2 3 Mass_mg 0.0000000013 0.0000000012 0.0000000018 0.000 lb/mmBtuO2 2.00E-13 1.87E-13 2.77E-13 0.000 ng/dscm 2.67E-04 2.49E-04 3.70E-04 0.000 ng/dscm@7%O2 2.32E-04 2.18E-04 3.21E-04 0.000 

### Compound:2,3,3',4,4',5,5'-HpCB (PCB189) Average RunNumber 1 2 3 Mass_mg 0.000000008 0.0000000157 0.0000000065 0.000 lb/mmBtuO2 1.23E-12 2.45E-12 1.00E-12 0.000 ng/dscm 1.64E-03 3.25E-03 1.33E-03 0.002 ng/dscm@7%O2 1.42E-03 2.84E-03 1.16E-03 0.002 

### Compound:2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC Average RunNumber 1 2 3 Mass_mg 0.000000174 0.00000031 0.0000000322 0.000 lb/mmBtuO2 2.68E-11 4.84E-11 4.95E-12 0.000 ng/dscm 3.57E-02 6.42E-02 6.61E-03 0.036 ng/dscm@7%O2 3.10E-02 5.61E-02 5.74E-03 0.031



### Monday, March 07, 2011 Page 8 of 24

### Compound:2,3,3',4,4'-PeCB (PCB105) Average RunNumber 1 2 3 Mass_mg 0.000000468 0.000000818 0.000000115 0.000 lb/mmBtuO2 7.20E-11 1.28E-10 1.77E-11 0.000 ng/dscm 9.61E-02 1.69E-01 2.36E-02 0.096 ng/dscm@7%O2 8.35E-02 1.48E-01 2.05E-02 0.084 

### Compound:2,3',4,4',5,5'-HxCB (PCB167) Average RunNumber 1 2 3 Mass_mg 0.0000000941 0.000000179 0.0000000175 0.000 lb/mmBtuO2 1.45E-11 2.80E-11 2.69E-12 0.000 ng/dscm 1.93E-02 3.71E-02 3.59E-03 0.020 ng/dscm@7%O2 1.68E-02 3.24E-02 3.12E-03 0.017 

### Compound:2,3,4,4',5-PeCB (PCB114) Average RunNumber 1 2 3 Mass_mg 0.0000000291 0.0000000448 0.000000006 0.000 lb/mmBtuO2 4.48E-12 7.00E-12 9.23E-13 0.000 ng/dscm 5.97E-03 9.28E-03 1.23E-03 0.005 ng/dscm@7%O2 5.19E-03 8.11E-03 1.07E-03 0.005 

### Compound:2,3',4,4',5-PeCB (PCB118) Average RunNumber 1 2 3 Mass_mg 0.00000148 0.00000288 0.000000339 0.000 lb/mmBtuO2 2.28E-10 4.50E-10 5.22E-11 0.000 ng/dscm 3.04E-01 5.97E-01 6.96E-02 0.324 ng/dscm@7%O2 2.64E-01 5.22E-01 6.05E-02 0.282 

### Compound:2',3,4,4',5-PeCB (PCB123) Average RunNumber 1 2 3 Mass_mg 0.0000000281 0.0000000516 0.0000000062 0.000 lb/mmBtuO2 4.32E-12 8.06E-12 9.54E-13 0.000 ng/dscm 5.77E-03 1.07E-02 1.27E-03 0.006 ng/dscm@7%O2 5.01E-03 9.35E-03 1.10E-03 0.005 

### Compound:2,3,4,6,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.0000000013 0.0000000014 0.0000000019 0.000 lb/mmBtuO2 2.00E-13 2.19E-13 2.92E-13 0.000 ng/dscm 2.67E-04 2.90E-04 3.90E-04 0.000 ng/dscm@7%O2 2.32E-04 2.54E-04 3.39E-04 0.000 

### Compound:2,3,4,7,8-PeCDF Average RunNumber 1 2 3 Mass_mg 0.0000000013 0.0000000027 0.0000000016 0.000 lb/mmBtuO2 2.00E-13 4.22E-13 2.46E-13 0.000



### Monday, March 07, 2011 Page 9 of 24ng/dscm 2.67E-04 5.59E-04 3.29E-04 0.000 ng/dscm@7%O2 2.32E-04 4.89E-04 2.86E-04 0.000 

### Compound:2,3,7,8-TCDD Average RunNumber 1 2 3 Mass_mg 0.0000000021 0.0000000017 0.0000000026 0.000 lb/mmBtuO2 3.23E-13 2.66E-13 4.00E-13 0.000 ng/dscm 4.31E-04 3.52E-04 5.34E-04 0.000 ng/dscm@7%O2 3.74E-04 3.08E-04 4.64E-04 0.000 

### Compound:2,3,7,8-TCDF Average RunNumber 1 2 3 Mass_mg 0.0000000013 0.0000000012 0.0000000017 0.000 lb/mmBtuO2 2.00E-13 1.87E-13 2.62E-13 0.000 ng/dscm 2.67E-04 2.49E-04 3.49E-04 0.000 ng/dscm@7%O2 2.32E-04 2.18E-04 3.03E-04 0.000 

### Compound:3,3',4,4',5,5'-HxCB (PCB169) Average RunNumber 1 2 3 Mass_mg 0.0000000093 0.000000018 0.0000000071 0.000 lb/mmBtuO2 1.43E-12 2.81E-12 1.09E-12 0.000 ng/dscm 1.91E-03 3.73E-03 1.46E-03 0.002 ng/dscm@7%O2 1.66E-03 3.26E-03 1.27E-03 0.002 

### Compound:3,3',4,4',5-PeCB (PCB126) Average RunNumber 1 2 3 Mass_mg 0.0000000329 0.000000072 0.0000000091 0.000 lb/mmBtuO2 5.06E-12 1.12E-11 1.40E-12 0.000 ng/dscm 6.75E-03 1.49E-02 1.87E-03 0.008 ng/dscm@7%O2 5.86E-03 1.30E-02 1.62E-03 0.007 

### Compound:3,3',4,4'-TCB (PCB77) Average RunNumber 1 2 3 Mass_mg 0.000000251 0.00000052 0.0000000628 0.000 lb/mmBtuO2 3.86E-11 8.12E-11 9.66E-12 0.000 ng/dscm 5.15E-02 1.08E-01 1.29E-02 0.057 ng/dscm@7%O2 4.47E-02 9.44E-02 1.12E-02 0.050 

### Compound:3,4,4',5-TCB (PCB81) Average RunNumber 1 2 3 Mass_mg 0.0000000125 0.0000000278 0.0000000119 0.000 lb/mmBtuO2 1.92E-12 4.34E-12 1.83E-12 0.000 ng/dscm 2.57E-03 5.76E-03 2.44E-03 0.004 ng/dscm@7%O2 2.23E-03 5.04E-03 2.12E-03 0.003 

### Compound:OCDD Average RunNumber 1 2 3 

### Monday, March 07, 2011 Page 10 of 24Mass_mg 0.0000000127 0.0000000149 0.0000000064 0.000 lb/mmBtuO2 1.95E-12 2.33E-12 9.85E-13 0.000 ng/dscm 2.61E-03 3.09E-03 1.31E-03 0.002 ng/dscm@7%O2 2.27E-03 2.70E-03 1.14E-03 0.002 

### Compound:OCDF Average RunNumber 1 2 3 Mass_mg 0.0000000037 0.000000013 0.0000000046 0.000 lb/mmBtuO2 5.69E-13 2.03E-12 7.08E-13 0.000 ng/dscm 7.60E-04 2.69E-03 9.44E-04 0.001 ng/dscm@7%O2 6.60E-04 2.35E-03 8.20E-04 0.001 

### Compound:Other HpCDD Average RunNumber 1 2 3 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 HpCDF Average RunNumber 1 2 3 Mass_mg 0 0.0000000037 0 0.000 lb/mmBtuO2 0.00E+00 5.78E-13 0.00E+00 0.000 ng/dscm 0.00E+00 7.66E-04 0.00E+00 0.000 ng/dscm@7%O2 0.00E+00 6.70E-04 0.00E+00 0.000 

### Compound:Other HxCDD Average RunNumber 1 2 3 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 HxCDF Average RunNumber 1 2 3 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 PeCDD Average RunNumber 1 2 3 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



### Monday, March 07, 2011 Page 11 of 24

### Compound:Other PeCDF Average RunNumber 1 2 3 Mass_mg 0 0.0000000134 0 0.000 lb/mmBtuO2 0.00E+00 2.09E-12 0.00E+00 0.000 ng/dscm 0.00E+00 2.78E-03 0.00E+00 0.001 ng/dscm@7%O2 0.00E+00 2.43E-03 0.00E+00 0.001 

### Compound:Other TCDD Average RunNumber 1 2 3 Mass_mg 0.0000000031 0.00000001 0.0000000035 0.000 lb/mmBtuO2 4.77E-13 1.56E-12 5.38E-13 0.000 ng/dscm 6.36E-04 2.07E-03 7.19E-04 0.001 ng/dscm@7%O2 5.53E-04 1.81E-03 6.25E-04 0.001 

### Compound:Other TCDF Average RunNumber 1 2 3 Mass_mg 0.0000000022 0.0000000421 0.0000000026 0.000 lb/mmBtuO2 3.38E-13 6.58E-12 4.00E-13 0.000 ng/dscm 4.52E-04 8.72E-03 5.34E-04 0.003 ng/dscm@7%O2 3.93E-04 7.62E-03 4.64E-04 0.003 

### Compound:Total Dioxins Average RunNumber 1 2 3 Mass_mg 0.0000000283 0.0000000367 0.0000000255 0.000 lb/mmBtuO2 4.35E-12 5.73E-12 3.92E-12 0.000 ng/dscm 5.81E-03 7.60E-03 5.24E-03 0.006 ng/dscm@7%O2 5.05E-03 6.64E-03 4.55E-03 0.005 

### Compound:Total Furans Average RunNumber 1 2 3 Mass_mg 0.0000000191 0.0000000874 0.000000025 0.000 lb/mmBtuO2 2.94E-12 1.37E-11 3.85E-12 0.000 ng/dscm 3.92E-03 1.81E-02 5.13E-03 0.009 ng/dscm@7%O2 3.41E-03 1.58E-02 4.46E-03 0.008 

### Compound:Total PCBs Average RunNumber 1 2 3 Mass_mg 0.000002587 0.0000049369 0.0000015608 0.000 lb/mmBtuO2 3.98E-10 7.71E-10 2.40E-10 0.000 ng/dscm 5.31E-01 1.02E+00 3.20E-01 0.624 ng/dscm@7%O2 4.61E-01 8.92E-01 2.78E-01 0.544 

### Compound:Total TEQ Average RunNumber 1 2 3 Mass_mg 0 0 0 0.000 lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000



### Monday, March 07, 2011 Page 12 of 24ng/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



### Location: Stack Exit - Method 29 Compound:Antimony Average RunNumber 1 2 3 Mass_mg 0.2761 0.39418 0.32215 0.331 Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000 lb/mmBtuO2 6.81E-05 9.39E-05 7.94E-05 0.000 mg/dscm 9.15E-02 1.28E-01 1.08E-01 0.109 mg/dscm@7%O2 7.90E-02 1.09E-01 9.21E-02 0.093 

### Compound:Arsenic Average RunNumber 1 2 3 Mass_mg 0.01033 0.01938 0.01078 0.013 Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000 lb/mmBtuO2 2.55E-06 4.62E-06 2.66E-06 0.000 mg/dscm 3.42E-03 6.28E-03 3.61E-03 0.004 mg/dscm@7%O2 2.95E-03 5.36E-03 3.08E-03 0.004 

### Compound:Beryllium Average RunNumber 1 2 3 Mass_mg 0.00179 0.002812 0.002312 0.002 Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000 lb/mmBtuO2 4.42E-07 6.70E-07 5.70E-07 0.000 mg/dscm 5.93E-04 9.11E-04 7.74E-04 0.001 mg/dscm@7%O2 5.12E-04 7.77E-04 6.60E-04 0.001 

### Compound:Cadmium Average RunNumber 1 2 3 Mass_mg 0.000309 0.000646 0.000619 0.001 Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000 lb/mmBtuO2 7.62E-08 1.54E-07 1.52E-07 0.000 mg/dscm 1.02E-04 2.09E-04 2.07E-04 0.000 mg/dscm@7%O2 8.81E-05 1.78E-04 1.77E-04 0.000 

### Compound:Chromium Average RunNumber 1 2 3 Mass_mg 0.0141 0.025 0.01699 0.019 Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000 lb/mmBtuO2 3.48E-06 5.96E-06 4.19E-06 0.000 mg/dscm 4.67E-03 8.10E-03 5.69E-03 0.006 mg/dscm@7%O2 4.03E-03 6.91E-03 4.85E-03 0.005 

### Compound:Filterable Particulate Average RunNumber 1 3 2 Mass_mg 86.7 87.9 152.5 109.033



### Monday, March 07, 2011 Page 13 of 24Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000 lb/mmBtuO2 2.14E-02 2.17E-02 3.63E-02 0.026 mg/dscm 2.87E+01 2.94E+01 4.94E+01 35.833 mg/dscm@7%O2 2.48E+01 2.51E+01 4.21E+01 30.667 

### Compound:Lead Average RunNumber 1 2 3 Mass_mg 0.0164 0.0263 0.02235 0.022 Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000 lb/mmBtuO2 4.05E-06 6.27E-06 5.51E-06 0.000 mg/dscm 5.43E-03 8.52E-03 7.49E-03 0.007 mg/dscm@7%O2 4.69E-03 7.27E-03 6.39E-03 0.006 

### Compound:Manganese Average RunNumber 1 2 3 Mass_mg 0.3188 0.5077 0.3038 0.377 Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000 lb/mmBtuO2 7.87E-05 1.21E-04 7.48E-05 0.000 mg/dscm 1.06E-01 1.65E-01 1.02E-01 0.124 mg/dscm@7%O2 9.15E-02 1.41E-01 8.70E-02 0.107 

### Compound:Nickel Average RunNumber 1 3 2 Mass_mg 2.114 1.9539 3.3352 2.468 Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000 lb/mmBtuO2 5.22E-04 4.81E-04 7.95E-04 0.001 mg/dscm 7.00E-01 6.54E-01 1.08E+00 0.811 mg/dscm@7%O2 6.04E-01 5.58E-01 9.21E-01 0.694 

### Compound:Selenium Average RunNumber 1 3 2 Mass_mg 0.0034 0.0086 0.007 0.006 Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000 lb/mmBtuO2 8.39E-07 2.12E-06 1.67E-06 0.000 mg/dscm 1.13E-03 2.88E-03 2.27E-03 0.002 mg/dscm@7%O2 9.76E-04 2.46E-03 1.94E-03 0.002



### Location: Stack Exit - OTM - 27/28 Compound:Filterable Particulate Average RunNumber 1 2 3 Mass_mg 45.9 58 43.4 49.100 lb/mmBtuO2 2.27E-02 3.51E-02 2.67E-02 0.028 

### Compound:Filterable PM2.5 Average RunNumber 1 2 3 Mass_mg 34.3 38 31.3 34.533 lb/mmBtuO2 1.70E-02 2.30E-02 1.92E-02 0.020



### Monday, March 07, 2011 Page 14 of 24

### Process Run Data

Compound:Inorganic (Aqueous) Condensible Pa Average RunNumber 1 2 3 Mass_mg 19.1 10.7 19.1 16.300 lb/mmBtuO2 9.45E-03 6.47E-03 1.17E-02 0.009 

### Compound:Organic Condensible Particulate Average RunNumber 1 2 3 Mass_mg 2.7 1.8 3 2.500 lb/mmBtuO2 1.34E-03 1.09E-03 1.84E-03 0.001 

### Compound:Total Particulate Average RunNumber 1 2 3 Mass_mg 67.7 70.5 65.5 67.900 lb/mmBtuO2 3.35E-02 4.27E-02 4.03E-02 0.039 

### Compound:Total PM2.5 Average RunNumber 1 2 3 Mass_mg 11.6 20 12.1 14.567 lb/mmBtuO2 5.74E-03 1.21E-02 7.44E-03 0.008



### Monday, March 07, 2011 Page 15 of 24

### Process Run Data



### Run Name Value UOM Comments Target Value 1 Coal Firing Rate 0 0 

### 2Coal Firing Rate 0 0 3 Coal Firing Rate 0 0 4Coal Firing Rate 0 0 

### 5 Coal Firing Rate 0 0 6Coal Firing Rate 0 0 7 Coal Firing Rate 0 0 

### 8 Coal Firing Rate 0 0 9 Coal Firing Rate 0 0 1 Average Heat Input 856.1 MMBtu/hr 0 

### 2Average Heat Input 862 MMBtu/hr 0 3 Average Heat Input 859.2 MMBtu/hr 0 4Average Heat Input 854.2 MMBtu/hr 0 

### 5 Average Heat Input 854.2 MMBtu/hr 0 6Average Heat Input 862 MMBtu/hr 0 7 Average Heat Input 854.2 MMBtu/hr 0 

### 8Average Heat Input 854.2 MMBtu/hr 0 9Average Heat Input 854.2 MMBtu/hr 0 1 Steam Output 624.31000 lb steam/hr 0 

### 2Steam Output 620.51000 lb steam/hr 0 3 Steam Output 623.51000 lb steam/hr 0 4 Steam Output 45.11000 lb steam/hr 0 

### 5 Steam Output 616.21000 lb steam/hr 0 6 Steam Output 620.51000 lb steam/hr 0 

### 7 Steam Output 616.21000 lb steam/hr 0 8 Steam Output 616.21000 lb steam/hr 0 9 Steam Output 616.21000 lb steam/hr 0 

### 1 Synfuel Firing Rate 0 0 2Synfuel Firing Rate 0 0 3 Synfuel Firing Rate 0 0 

### 4 Synfuel Firing Rate 0 0 5 Synfuel Firing Rate 0 0 6 Synfuel Firing Rate 0 0



### Monday, March 07, 2011 Page 16 of 24

### 7 Synfuel Firing Rate 0 0



### 8 Synfuel Firing Rate 0 0 9 Synfuel Firing Rate 0 0 1 Petroleum Coke Firing Rate 0 0 

### 2Petroleum Coke Firing Rate 0 0 3 Petroleum Coke Firing Rate 0 0 4Petroleum Coke Firing Rate 0 0 

### 5Petroleum Coke Firing Rate 0 0 6Petroleum Coke Firing Rate 0 0 7Petroleum Coke Firing Rate 0 0 

### 8Petroleum Coke Firing Rate 0 0 9Petroleum Coke Firing Rate 0 0 1 Coal Gas Firing Rate 0 0 

### 2Coal Gas Firing Rate 0 0 3 Coal Gas Firing Rate 0 0 4Coal Gas Firing Rate 0 0 

### 5 Coal Gas Firing Rate 0 0 6Coal Gas Firing Rate 0 0 7 Coal Gas Firing Rate 0 0 

### 8 Coal Gas Firing Rate 0 0 9 Coal Gas Firing Rate 0 0 

### 1 Fuel Oil Firing Rate 0 0 2Fuel Oil Firing Rate 0 0 3 Fuel Oil Firing Rate 0 0 

### 4Fuel Oil Firing Rate 0 0 5 Fuel Oil Firing Rate 0 0 6Fuel Oil Firing Rate 0 0 

### 7Fuel Oil Firing Rate 0 0 8Fuel Oil Firing Rate 0 0 9Fuel Oil Firing Rate 0 0 

### 1 Flue Gas Flow Rate 0 dscfm 0 2Flue Gas Flow Rate 0 dscfm 0 3 Flue Gas Flow Rate 0 dscfm 0 

### 4Flue Gas Flow Rate 0 dscfm 0 5 Flue Gas Flow Rate 0 dscfm 0 6Flue Gas Flow Rate 0 dscfm 0



### Monday, March 07, 2011 Page 17 of 24

### 7Flue Gas Flow Rate 0 dscfm 0



### 8Flue Gas Flow Rate 0 dscfm 0 9Flue Gas Flow Rate 0 dscfm 0 1 Pressure Drop Across FGD (if applicable) 0 in H20 0 

### 2Pressure Drop Across FGD (if applicable) 0 in H20 0 3 Pressure Drop Across FGD (if applicable) 0 in H20 0 4Pressure Drop Across FGD (if applicable) 0 in H20 0 

### 5 Pressure Drop Across FGD (if applicable) 0 in H20 0 6Pressure Drop Across FGD (if applicable) 0 in H20 0 7 Pressure Drop Across FGD (if applicable) 0 in H20 0 

### 8Pressure Drop Across FGD (if applicable) 0 in H20 0 9Pressure Drop Across FGD (if applicable) 0 in H20 0 1 FGD Scrubber Liquor pH 0 pH 0 

### 2FGD Scrubber Liquor pH 0 pH 0 3 FGD Scrubber Liquor pH 0 pH 0 4FGD Scrubber Liquor pH 0 pH 0 

### 5 FGD Scrubber Liquor pH 0 pH 0 6FGD Scrubber Liquor pH 0 pH 0 7FGD Scrubber Liquor pH 0 pH 0 

### 8FGD Scrubber Liquor pH 0 pH 0 9FGD Scrubber Liquor pH 0 pH 0 

### 1 FGD Scrubber Liquor Flow Rate 0 gal/min 0 2FGD Scrubber Liquor Flow Rate 0 gal/min 0 3 FGD Scrubber Liquor Flow Rate 0 gal/min 0 

### 4FGD Scrubber Liquor Flow Rate 0 gal/min 0 5 FGD Scrubber Liquor Flow Rate 0 gal/min 0 6FGD Scrubber Liquor Flow Rate 0 gal/min 0 

### 7FGD Scrubber Liquor Flow Rate 0 gal/min 0 8FGD Scrubber Liquor Flow Rate 0 gal/min 0 9FGD Scrubber Liquor Flow Rate 0 gal/min 0 

### 1 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0

2 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0



### 3 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0

4 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0



### Monday, March 07, 2011 Page 18 of 24

### 5 Sorbent Type and Sorbent Injection Rate (if

applicable) 0 lb/hr 0



### 6 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0

7 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0

8 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0



### 9 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0

1 Flue Gas Oxygen Content 0 % 0 2Flue Gas Oxygen Content 0 % 0 

### 3 Flue Gas Oxygen Content 0 % 0 4Flue Gas Oxygen Content 0 % 0 5 Flue Gas Oxygen Content 0 % 0 

### 6Flue Gas Oxygen Content 0 % 0 7Flue Gas Oxygen Content 0 % 0 8Flue Gas Oxygen Content 0 % 0 

### 9Flue Gas Oxygen Content 0 % 0 1 Flue Gas Carbon Dioxide Content 0 % 0 2Flue Gas Carbon Dioxide Content 0 % 0 

### 3 Flue Gas Carbon Dioxide Content 0 % 0 4Flue Gas Carbon Dioxide Content 0 % 0 5 Flue Gas Carbon Dioxide Content 0 % 0 

### 6Flue Gas Carbon Dioxide Content 0 % 0 7Flue Gas Carbon Dioxide Content 0 % 0 8Flue Gas Carbon Dioxide Content 0 % 0 

### 9Flue Gas Carbon Dioxide Content 0 % 0 1 Flue Gas Moisture Content 0 % 0 

### 2Flue Gas Moisture Content 0 % 0 3 Flue Gas Moisture Content 0 % 0 4Flue Gas Moisture Content 0 % 0 

### 5 Flue Gas Moisture Content 0 % 0 6Flue Gas Moisture Content 0 % 0 7Flue Gas Moisture Content 0 % 0 

### 8Flue Gas Moisture Content 0 % 0 9Flue Gas Moisture Content 0 % 0 1 Flue Gas Sampling Point Temperature 0 Deg F 0



### Monday, March 07, 2011 Page 19 of 24

### 2Flue Gas Sampling Point Temperature 0 Deg F 0



### 3 Flue Gas Sampling Point Temperature 0 Deg F 0 4Flue Gas Sampling Point Temperature 0 Deg F 0 5 Flue Gas Sampling Point Temperature 0 Deg F 0 

### 6Flue Gas Sampling Point Temperature 0 Deg F 0 7Flue Gas Sampling Point Temperature 0 Deg F 0 8Flue Gas Sampling Point Temperature 0 Deg F 0 

### 9Flue Gas Sampling Point Temperature 0 Deg F 0 1 Flue Gas Pressure 0 atm 0 2Flue Gas Pressure 0 atm 0 

### 3 Flue Gas Pressure 0 atm 0 4Flue Gas Pressure 0 atm 0 5 Flue Gas Pressure 0 atm 0 

### 6Flue Gas Pressure 0 atm 0 7Flue Gas Pressure 0 atm 0 8Flue Gas Pressure 0 atm 0 

### 9Flue Gas Pressure 0 atm 0 1 Standard Pressure 0 atm 0 2 Standard Pressure 0 atm 0 

### 3 Standard Pressure 0 atm 0 4 Standard Pressure 0 atm 0 

### 5 Standard Pressure 0 atm 0 6 Standard Pressure 0 atm 0 7 Standard Pressure 0 atm 0 

### 8 Standard Pressure 0 atm 0 9 Standard Pressure 0 atm 0 1 Standard Temperature 0 Deg F 0 

### 2Standard Temperature 0 Deg F 0 3 Standard Temperature 0 Deg F 0 4 Standard Temperature 0 Deg F 0 

### 5 Standard Temperature 0 Deg F 0 6 Standard Temperature 0 Deg F 0 7 Standard Temperature 0 Deg F 0 

### 8 Standard Temperature 0 Deg F 0 9 Standard Temperature 0 Deg F 0 1 Unit Gross Electrical Output 90.4 MW 0



### Monday, March 07, 2011 Page 20 of 24

### APCD Run Data

Process Lab Run Data 2Unit Gross Electrical Output 91 MW 0 

### 3 Unit Gross Electrical Output 90.6 MW 0 4Unit Gross Electrical Output 89.8 MW 0 5 Unit Gross Electrical Output 89.8 MW 0 

### 6Unit Gross Electrical Output 91 MW 0 7 Unit Gross Electrical Output 89.8 MW 0 8Unit Gross Electrical Output 89.8 MW 0 

### 9Unit Gross Electrical Output 89.8 MW 0 1 Unit Net Electric Generation 0 MWh 0 2Unit Net Electric Generation 0 MWh 0 

### 3 Unit Net Electric Generation 0 MWh 0 4Unit Net Electric Generation 0 MWh 0 5 Unit Net Electric Generation 0 MWh 0 

### 6Unit Net Electric Generation 0 MWh 0 7 Unit Net Electric Generation 0 MWh 0 8Unit Net Electric Generation 0 MWh 0 

### 9Unit Net Electric Generation 0 MWh 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 ValueUOM Comments 

### 1 See 4b Comments. 0

Monday, March 07, 2011 Page 21 of 24

### Sampling / Stack Data Results Detail



### LocationStack Exit - Method 23 Average Run Number 1 2 3 Test Date 10/25/201010/27/2010 10/28/2010 Run Start Time 8:29:00 AM8:52:00 AM8:29:00 AM Run Finish Time 4:57:00 PM5:02:00 PM4:57:00 PM Net Traversing Points 48 48 48 Net Run Time, minutes 480 480 480 Nozzle Diameter, inches 0.185 0.185 0.185 0.185 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.985 0.985 0.985 0.985 Barometric Pressure, inches of Mercury 29.84 29.85 29.84 29.843 Average Orifice Meter Differential, inches H2O 0.41 0.40 0.41 0.407 Dry Gas Meter Volume Sampled, cubic feet 181.869 180.067 181.869 181.268 Average Dry Gas Meter Temperature, °F 88.92 88.48 88.92 88.773 Dry Gas Meter Volume Sampled, dscf 172.027 170.512 172.027 171.522 Total Moisture Liquid collected, g 461 439 461 453.667 Volume of Water Vapor, standard cubic feet 21.70 20.66 21.70 21.353 Moisture Content of Stack Gas, % 11.20 10.81 11.20 11.070 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.888 0.8919 0.888 0.889 Carbon Dioxide, % 12.8 12.8 12.8 12.800 Oxygen, % 4.9 5 4.9 4.933 Carbon Monoxide & Nitrogen, % 82.3 82.2 82.3 82.267 Fuel Factor 1.25 1.24 1.25 Dry Molecular Weight, lb/lb-Mole 30.24 30.25 30.24 30.243 Wet Molecular weight, lb/lb-Mole 28.87 28.93 28.87 28.890 Flue Gas Static Pressure, inches of H2O 1 1 1 1.000 Absolute Flue Gas Pressure, inches of Mercury 29.91 29.92 29.91 29.913 Average Stack Gas Temperature, °F 291.08 291.98 291.08 291.380 Average Velocity Head, inches of H2O 0.5809207513 020410.549666828

4376650.580920751

30204 0.571 Average Stack Gas Velocity, feet/second 51.05 49.62 51.05 50.573 Stack Cross-Sectional Area, square feet 0.000 0.000 0.000 0.000 Dry Volumetric Flow Rate, dry scfm 0.0 0.0 0.0 0.000 Actual Wet Volumetric Flue Gas Flow Rate, acfm 0.0 0.0 0.0 0.000 Percent Isokinetic of Sampling Rate, % 100.4 102.1 100.4 100.967 Percent Excess Air, % 29.1 29.9 29.1 29.367 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Round Duct Diameter, inches 0 0 0 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0 Fw 10320 10320 1032010,320.000 Fc 1420 1420 14201,420.000



### Monday, March 07, 2011 Page 22 of 24

### LocationStack Exit - Method 29 Average

Run Number 1 2 3 Test Date 10/26/201010/26/2010 10/27/2010 Run Start Time 8:52:00 AM1:40:00 PM8:49:00 AM Run Finish Time 1:05:00 PM5:53:00 PM1:02:00 PM Net Traversing Points 24 24 24 Net Run Time, minutes 240 240 240 Nozzle Diameter, inches 0.204 0.204 0.204 0.204 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 1.02 1.02 1.02 1.020 Barometric Pressure, inches of Mercury 29.8 29.95 29.82 29.857 Average Orifice Meter Differential, inches H2O 0.67 0.70 0.67 0.680 Dry Gas Meter Volume Sampled, cubic feet 108.270 110.070 107.791 108.710 Average Dry Gas Meter Temperature, °F 85.73 85.29 89.58 86.867 Dry Gas Meter Volume Sampled, dscf 106.595 109.008 105.450 107.018 Total Moisture Liquid collected, g 292.1 324 287.3 301.133 Volume of Water Vapor, standard cubic feet 13.75 15.25 13.52 14.173 Moisture Content of Stack Gas, % 11.43 12.27 11.36 11.687 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.8857 0.8773 0.8864 0.883 Carbon Dioxide, % 13 13.1 13 13.033 Oxygen, % 4.8 4.6 4.6 4.667 Carbon Monoxide & Nitrogen, % 82.2 82.3 82.4 82.300 Fuel Factor 1.24 1.24 1.25 Dry Molecular Weight, lb/lb-Mole 30.27 30.28 30.26 30.270 Wet Molecular weight, lb/lb-Mole 28.87 28.77 28.87 28.837 Flue Gas Static Pressure, inches of H2O 1 1 1 1.000 Absolute Flue Gas Pressure, inches of Mercury 29.87 30.02 29.89 29.927 Average Stack Gas Temperature, °F 290.17 293.42 290.00 291.197 Average Velocity Head, inches of H2O 0.5763274451 622850.603513008

9564340.575664917

249972 0.585 Average Stack Gas Velocity, feet/second 50.85 52.11 50.80 51.253 Stack Cross-Sectional Area, square feet 0.000 0.000 0.000 0.000 Dry Volumetric Flow Rate, dry scfm 0.0 0.0 0.0 0.000 Actual Wet Volumetric Flue Gas Flow Rate, acfm 0.0 0.0 0.0 0.000 Percent Isokinetic of Sampling Rate, % 103.1 103.8 101.9 102.933 Percent Excess Air, % 28.4 26.9 26.8 27.367 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Round Duct Diameter, inches 0 0 0 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0 Fw 10320 10320 1032010,320.000 Fc 1420 1420 14201,420.000



### Monday, March 07, 2011 Page 23 of 24

### LocationStack Exit - OTM - 27/28 Average

Run Number 1 2 3 Test Date 10/26/201010/26/2010 10/26/2010 Run Start Time 9:06:00 AM12:08:00 PM3:49:00 PM Run Finish Time 11:38:00 AM2:28:00 PM5:57:00 PM Net Traversing Points 27 28 26 Net Run Time, minutes 120 120 120 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 0.985 0.985 0.985 0.985 Barometric Pressure, inches of Mercury 29.8 29.95 29.95 29.900 Average Orifice Meter Differential, inches H2O 0.46 0.46 0.46 0.460 Dry Gas Meter Volume Sampled, cubic feet 56.923 47.625 45.184 49.911 Average Dry Gas Meter Temperature, °F 88.13 89.75 83.42 87.100 Dry Gas Meter Volume Sampled, dscf 53.854 45.151 43.336 47.447 Total Moisture Liquid collected, g 127.4 129.4 122.7 126.500 Volume of Water Vapor, standard cubic feet 6.00 6.09 5.78 5.957 Moisture Content of Stack Gas, % 10.02 11.89 11.77 11.227 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.8998 0.8811 0.8823 0.888 Carbon Dioxide, % 12.7 12.4 12.8 12.633 Oxygen, % 5 5.4 5 5.133 Carbon Monoxide & Nitrogen, % 82.3 82.2 82.2 82.233 Fuel Factor 1.25 1.25 1.24 Dry Molecular Weight, lb/lb-Mole 30.23 30.20 30.25 30.227 Wet Molecular weight, lb/lb-Mole 29.00 28.75 28.81 28.853 Flue Gas Static Pressure, inches of H2O 1 1 1 1.000 Absolute Flue Gas Pressure, inches of Mercury 29.87 30.02 30.02 29.970 Average Stack Gas Temperature, °F 292.08 294.75 289.75 292.193 Average Velocity Head, inches of H2O 0.6739772661 43070.656948501

6109470.599519559

561124 0.643 Average Stack Gas Velocity, feet/second 54.93 54.43 51.77 53.710 Stack Cross-Sectional Area, square feet 0.000 0.000 0.000 0.000 Dry Volumetric Flow Rate, dry scfm 0.0 0.0 0.0 0.000 Actual Wet Volumetric Flue Gas Flow Rate, acfm 0.0 0.0 0.0 0.000 Percent Isokinetic of Sampling Rate, % 114.4 98.7 98.8 103.967 Percent Excess Air, % 29.9 33.1 29.9 30.967 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Round Duct Diameter, inches 0 0 0 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0 Fw 10320 10320 1032010,320.000 Fc 1420 1420 14201,420.000



### Monday, March 07, 2011 Page 24 of 24