### Name:

Title: Company: Sign Date: Name: Title: Company: Sign Date: Permitted Facility Representative / Date Testing Company Representative / Date



## Northampton Generating Company, LP EPA MACT

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.

Tuesday, March 01, 2011 Page 1 of 22

### Northampton Generating Company, LP EPA MACT

Facility Information: Northampton Generating Company, LP
1 Horwith Drive

Northampton PA18067 Contact:Daniel Traynor Phone:(610)261-3073 Fax: Email: DanielTraynor@cogentrix.com Testing Company: AirNova, Inc. 5845 Clayton Avenue

Pennsauken NJ08109 Contact:Lenny D. Katerynczuk Phone:856-486-1500 Fax: 856-486-9896 Email: lenny@airnova.com

Air Permit Number: 48-306-012 Permitted Source ID/Name: Unit 1 50888 Permitted Maximum Process Rate: 1146.000 MMBTU/Hr Max. Normal Operation Process Rate: 108MW Target Process Test Rate 108MW

Description of the source (including control equipment). Please see the attachments for source or process flow diagram: Northampton Generating Company, LP operates a 112 MW anthracite waste coal-fired electric facility in Northampton County, Pennsylvania. The facility utilizes CFB technology to cleanly and efficiently converty low value, low cost waste coal into power. Industry/SCC/NAIS221112

Sampling Location Information:

Test Parameter Information: AFS #:4209500230 FRS #:110006623396

SCC / Description10102018 External Combustion Boilers - Electric Generation - Waste Coal - Circulating Fluidized Bed Combustion

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 Unit 1 114 1440 960 4 0 12 0 0

Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location Carbon Monoxide Method 10 3 127 0 Unit 1 Formaldehyde Method 0011 3 127 0 Unit 1 Total organic compounds

(TOC) as Propane Method 25A 3 127 0 Unit 1
Hydrogen Fluoride Method 26A 3 185 0 Unit 1 Regulation Description Compound Limit Unit Clean Air Act Section 112 0 Utility Boiler MACT ICR 0



### Tuesday, March 01, 2011 Page 2 of 22

### Northampton Generating Company, LP EPA MACT

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.

Hydrogen Chloride Method 26A 3 185 0 Unit 1 Inorganic (Aqueous)

Condensible Part. OTM - 27/28 3 373 0 Unit 1
Organic Condensible

Particulate OTM - 27/28 3 373 0 Unit 1

Total PM2.5 OTM - 27/28 3 373 0 Unit 1 Filterable PM2.5 OTM - 27/28 3 373 0 Unit 1 Manganese Method 29 3 373 0 Unit 1 Antimony Method 29 3 373 0 Unit 1 Arsenic Method 29 3 373 0 Unit 1 Beryllium Method 29 3 373 0 Unit 1 Cadmium Method 29 3 373 0 Unit 1 Chromium Method 29 3 373 0 Unit 1 Lead Method 29 3 373 0 Unit 1 Mercury Method 29 3 373 0 Unit 1 Nickel Method 29 3 373 0 Unit 1 Selenium Method 29 3 373 0 Unit 1 Cobalt Method 29 3 373 0 Unit 1 Filterable Particulate Method 5 3 373 0 Unit 1 Sulfur Dioxide Method 6C 3 185 0 Unit 1 Nitrogen oxides (NOx) Method 7E 3 185 0 Unit 1



### Tuesday, March 01, 2011 Page 3 of 22

### Northampton Generating Company, LP EPA MACT

Sampling / Stack Data Results Summary



### Location Unit 1 - Method 0011 Average Run Number 1 2 3
Test Date 3/24/2010 3/24/2010 3/24/2010 Run Start Time 1:32:00 PM4:01:00 PM 6:15:00 PM
Run Finish Time 3:40:00 PM6:08:00 PM 8:22:00 PM Net Run Time, minutes 120 120 120 Dry Gas Meter Volume Sampled, dscf 81.186 88.371 84.341 84.633 Moisture Content of Stack Gas, % 6.84 7.00 7.57 7.137 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 15.35 15.54 15.13 15.340 Oxygen, % 5.34 5.33 5.66 5.443 Average Stack Gas Temperature, °F 320.08 326.08 328.33 324.830 Dry Volumetric Flow Rate, dry scfm 279,631.3 287,632.4 281,586.2 282,949.967 Actual Wet Volumetric Flue Gas Flow Rate, acfm 446,301.4 463,398.2 457,146.4 455,615.333 Percent Isokinetic of Sampling Rate, % 97.0 102.7 100.1 99.933 F-Factor, dscfm/MMBtu @ %O2 10204 10345 10483 10,344.000
Fw 0 0 0 0.000
Fc 0 0 0 0.000



### Location Unit 1 - Method 10 Average Run Number 1 2 3
Test Date 3/24/2010 3/24/2010 3/24/2010 Run Start Time 1:32:00 PM4:01:00 PM 6:15:00 PM
Run Finish Time 3:40:00 PM6:08:00 PM 8:22:00 PM Carbon Dioxide, % 15.35 15.54 15.13 15.340 Oxygen, % 5.34 5.33 5.66 5.443 Dry Volumetric Flow Rate, dry scfm 279523 287529 281473 282,841.667 F-Factor, dscfm/MMBtu @ %O2 10204 10345 10483 10,344.000 Moisture, % 6.8 7 7.6 7.133 Fuel Type Override Override Override
Fw 0 0 0 0.000
Fc 0 0 0 0.000



### Tuesday, March 01, 2011 Page 4 of 22

### Northampton Generating Company, LP EPA MACT

Location Unit 1 - Method 25A Average Run Number 1 2 3
Test Date 3/24/2010 3/24/2010 3/24/2010 Run Start Time 1:32:00 PM4:01:00 PM 6:15:00 PM
Run Finish Time 3:40:00 PM6:08:00 PM 8:22:00 PM Carbon Dioxide, % 15.35 15.54 15.13 15.340 Oxygen, % 5.34 5.33 5.66 5.443 Dry Volumetric Flow Rate, dry scfm 279523 287529 281473 282,841.667 F-Factor, dscfm/MMBtu @ %O2 10204 10345 10483 10,344.000 Moisture, % 6.84 7 7.6 7.147 Fuel Type Override Override Override
Fw 0 0 0 0.000
Fc 0 0 0 0.000



### Location Unit 1 - Method 26A Average Run Number 1 2 3
Test Date 3/25/2010 3/25/2010 3/25/2010 Run Start Time 6:55:00 AM 10:19:00 AM 1:40:00 PM

Run Finish Time 10:00:00 AM1:25:00 PM 4:45:00 PM Net Run Time, minutes 180 180 180 Dry Gas Meter Volume Sampled, dscf 131.702 125.080 125.721 127.501 Moisture Content of Stack Gas, % 7.48 7.72 7.96 7.720 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 15.33 15.32 15.13 15.260 Oxygen, % 5.61 5.3 5.17 5.360 Average Stack Gas Temperature, °F 313.75 317.58 322.92 318.083 Dry Volumetric Flow Rate, dry scfm 300,011.2 286,563.1 284,021.9 290,198.733 Actual Wet Volumetric Flue Gas Flow Rate, acfm 475,986.8 458,549.8 458,337.2 464,291.267 Percent Isokinetic of Sampling Rate, % 97.8 97.3 98.6 97.900 F-Factor, dscfm/MMBtu @ %O2 10528 10584 10640 10,584.000
Fw 0 0 0 0.000
Fc 0 0 0 0.000



### Tuesday, March 01, 2011 Page 5 of 22

### Northampton Generating Company, LP EPA MACT

Location Unit 1 - Method 29 Average Run Number 1 2 3
Test Date 3/23/2010 3/23/2010 3/24/2010 Run Start Time 7:30:00 AM2:32:00 PM 6:40:00 AM
Run Finish Time 1:45:00 PM8:48:00 PM12:50:00 PM Net Run Time, minutes 360 360 360 Dry Gas Meter Volume Sampled, dscf 197.825 187.041 192.133 192.333 Moisture Content of Stack Gas, % 8.14 8.31 7.03 7.827 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 14.5 15.3 15.68 15.160 Oxygen, % 5.43 5.4 5.36 5.397 Average Stack Gas Temperature, °F 322.83 324.83 307.42 318.360 Dry Volumetric Flow Rate, dry scfm 290,654.2 271,806.7 281,739.0 281,399.967 Actual Wet Volumetric Flue Gas Flow Rate, acfm 477,092.6 449,193.4 445,068.1 457,118.033 Percent Isokinetic of Sampling Rate, % 96.0 97.0 96.2 96.400 F-Factor, dscfm/MMBtu @ %O2 10412 10215 10559 10,395.333
Fw 0 0 0 0.000
Fc 0 0 0 0.000



### Location Unit 1 - Method 5 Average Run Number 1 2 3
Test Date 3/23/2010 3/23/2010 3/24/2010 Run Start Time 7:30:00 AM2:32:00 PM 6:40:00 AM Run Finish Time 1:45:00 PM8:48:00 PM12:50:00 PM Net Run Time, minutes 360 360 360 Dry Gas Meter Volume Sampled, dscf 197.825 187.041 192.133 192.333 Moisture Content of Stack Gas, % 8.14 8.31 7.03 7.827 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 14.5 15.3 15.68 15.160 Oxygen, % 5.43 5.4 5.36 5.397 Average Stack Gas Temperature, °F 322.83 324.75 307.42 318.333 Dry Volumetric Flow Rate, dry scfm 290,654.2 271,834.4 281,739.0 281,409.200 Actual Wet Volumetric Flue Gas Flow Rate, acfm 477,092.6 449,193.4 445,068.1 457,118.033 Percent Isokinetic of Sampling Rate, % 96.0 97.0 96.2 96.400 F-Factor, dscfm/MMBtu @ %O2 10412 10215 10559 10,395.333
Fw 0 0 0 0.000
Fc 0 0 0 0.000



### Tuesday, March 01, 2011 Page 6 of 22

### Northampton Generating Company, LP EPA MACT

Location Unit 1 - Method 6C Average Run Number 1 2 3
Test Date 3/25/2010 3/25/2010 3/25/2010 Run Start Time 10:19:00 AM 10:19:00 AM 1:40:00 PM

Run Finish Time 1:25:00 PM1:25:00 PM 4:45:00 PM Carbon Dioxide, % 15.33 15.32 15.13 15.260 Oxygen, % 5.61 5.3 5.17 5.360 Dry Volumetric Flow Rate, dry scfm 299903 286451 284905 290,419.667 F-Factor, dscfm/MMBtu @ %O2 10528 10584 10640 10,584.000 Moisture, % 7.5 7.7 8 7.733 Fuel Type Override Override Override
Fw 0 0 0.000
Fc 1800 0 0 600.000



### Location Unit 1 - Method 7E Average Run Number 1 2 3
Test Date 3/25/2010 3/25/2010 3/25/2010 Run Start Time 6:55:00 AM 10:19:00 AM 1:40:00 PM

Run Finish Time 10:00:00 AM1:25:00 PM 4:45:00 PM Carbon Dioxide, % 15.33 15.32 15.13 15.260 Oxygen, % 5.61 5.3 5.17 5.360 Dry Volumetric Flow Rate, dry scfm 299903 286451 284905 290,419.667 F-Factor, dscfm/MMBtu @ %O2 10528 10584 10640 10,584.000 Moisture, % 7.5 7.7 8 7.733 Fuel Type Override Override Override
Fw 0 0 0 0.000
Fc 0 0 0 0.000



### Tuesday, March 01, 2011 Page 7 of 22

### Northampton Generating Company, LP EPA MACT

Location Unit 1 - OTM - 27/28 Average Run Number 1 2 3
Test Date 3/23/2010 3/23/2010 3/24/2010 Run Start Time 7:30:00 AM2:32:00 PM 6:40:00 AM
Run Finish Time 1:44:00 PM8:45:00 PM12:50:00 PM Net Run Time, minutes 358.9 358.4 360 Dry Gas Meter Volume Sampled, dscf 127.812 128.114 131.030 128.985 Moisture Content of Stack Gas, % 7.92 8.15 6.75 7.607 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 14.5 15.3 15.68 15.160 Oxygen, % 5.43 5.4 5.36 5.397 Average Stack Gas Temperature, °F 320.08 322.75 312.17 318.333 Dry Volumetric Flow Rate, dry scfm 295,661.4 293,191.7 301,272.1 296,708.400 Actual Wet Volumetric Flue Gas Flow Rate, acfm 482,451.2 482,408.7 477,432.8 480,764.233 Percent Isokinetic of Sampling Rate, % 100.2 101.4 100.5 100.700 F-Factor, dscfm/MMBtu @ %O2 10412 10215 10559 10,395.333
Fw 0 0 0 0.000
Fc 0 0 0 0.000



### Tuesday, March 01, 2011 Page 8 of 22

### Northampton Generating Company, LP EPA MACT

Emissions Summary



### Location: Unit 1 - Method 0011 Compound: Formaldehyde Average RunNumber 1 2 3 Mass_mg 0.0044 0.00424 0.0043 0.004 Elb/hr 2.00E-03 1.83E-03 1.90E-03 0.002 lb/mmBtuO2 1.64E-06 1.47E-06 1.62E-06 0.000 ppm 1.53E-03 1.36E-03 1.44E-03 0.001 ppm@7%O2 1.37E-03 1.21E-03 1.31E-03 0.001



### Location: Unit 1 - Method 10 Compound: Carbon Monoxide Average Run 1 2 3 Elb/hr 1.28E+02 1.34E+02 1.36E+02 132.667 lb/mmBtuO2 1.05E-01 1.08E-01 1.15E-01 0.109 ppm 1.05E+02 1.07E+02 1.10E+02 107.333 ppm@7%O2 9.38E+01 9.55E+01 1.00E+02 96.433



### Location: Unit 1 - Method 25A 

### Compound: Total organic compounds (TOC) as Average Run 1 2 3 Elb/hr 5.57E-01 1.82E-01 7.12E-01 0.484 lb/mmBtuO2 4.55E-04 1.46E-04 6.07E-04 0.000 ppm 2.90E-01 9.21E-02 3.69E-01 0.250 ppm@7%O2 2.59E-01 8.22E-02 3.37E-01 0.226



### Location: Unit 1 - Method 26A Compound: Hydrogen Chloride Average RunNumber 1 2 3 Mass_mg 124 102 95.1 107.033 Elb/hr 3.74E+01 3.09E+01 2.84E+01 32.233 lb/mmBtuO2 2.99E-02 2.55E-02 2.36E-02 0.026 ppm 2.19E+01 1.90E+01 1.76E+01 19.500 

### Compound: Hydrogen Fluoride Average RunNumber 1 2 3 Mass_mg 2.54 3.03 1.53 2.367 Elb/hr 7.65E-01 9.18E-01 4.57E-01 0.713 lb/mmBtuO2 6.12E-04 7.57E-04 3.79E-04 0.001 ppm 8.19E-01 1.03E+00 5.17E-01 0.789



### Location: Unit 1 - Method 29 Compound: Antimony Average RunNumber 1 2 3



### Tuesday, March 01, 2011 Page 9 of 22

### Northampton Generating Company, LP EPA MACT

Mass_mg 0.001795 0.000194 0.000271 0.001 lb/mmBtuO2 2.81E-07 3.15E-08 4.42E-08 0.000 

### Compound: Arsenic Average RunNumber 1 2 3 Mass_mg 0.000381 0.000261 0.000188 0.000 lb/mmBtuO2 5.97E-08 4.24E-08 3.06E-08 0.000 

### Compound: Beryllium Average RunNumber 1 2 3 Mass_mg 0.000025 0.000025 0.000025 0.000 lb/mmBtuO2 3.92E-09 4.06E-09 4.07E-09 0.000 

### Compound: Cadmium Average RunNumber 1 2 3 Mass_mg 0.000147 0.000568 0.0001 0.000 lb/mmBtuO2 2.30E-08 9.22E-08 1.63E-08 0.000 

### Compound: Chromium Average RunNumber 1 2 3 Mass_mg 0.00303 0.002621 0.002557 0.003 lb/mmBtuO2 4.75E-07 4.26E-07 4.17E-07 0.000 

### Compound: Cobalt Average RunNumber 1 2 3 Mass_mg 0.00016 0.00019 0.000154 0.000 lb/mmBtuO2 2.51E-08 3.08E-08 2.51E-08 0.000 

### Compound: Lead Average RunNumber 1 2 3 Mass_mg 0.001652 0.001313 0.001607 0.002 lb/mmBtuO2 2.59E-07 2.13E-07 2.62E-07 0.000 

### Compound: Manganese Average RunNumber 1 2 3 Mass_mg 0.00369 0.003203 0.003319 0.003 lb/mmBtuO2 5.78E-07 5.20E-07 5.41E-07 0.000 

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

### Compound: Nickel Average RunNumber 1 2 3


### Tuesday, March 01, 2011 Page 10 of 22

### Northampton Generating Company, LP EPA MACT

Mass_mg 0.00244 0.001954 0.001874 0.002 lb/mmBtuO2 3.83E-07 3.17E-07 3.05E-07 0.000 

### Compound: Selenium Average RunNumber 1 2 3 Mass_mg 0.0001 0.0001 0.0001 0.000 lb/mmBtuO2 1.57E-08 1.62E-08 1.63E-08 0.000



### Location: Unit 1 - Method 5 

### Compound: Filterable Particulate Average RunNumber 1 2 3 Mass_mg 46.1 58.7 59.2 54.667 Elb/hr 8.96E+00 1.13E+01 1.15E+01 10.587 gr/dscf 3.60E-03 4.84E-03 4.76E-03 0.004 lb/mmBtuO2 7.23E-03 9.53E-03 9.65E-03 0.009



### Location: Unit 1 - Method 6C Compound: Sulfur Dioxide Average Run 1 2 3 Elb/hr 1.49E+02 1.46E+02 1.59E+02 151.333 lb/mmBtuO2 1.19E-01 1.21E-01 1.31E-01 0.124 ppm 4.97E+01 5.12E+01 5.58E+01 52.233 ppm@7%O2 4.52E+01 4.56E+01 4.93E+01 46.700



### Location: Unit 1 - Method 7E Compound: Nitrogen oxides (NOx) Average Run 1 2 3 Elb/hr 1.20E+02 1.01E+02 1.14E+02 111.667 lb/mmBtuO2 9.60E-02 8.33E-02 9.41E-02 0.091 ppm 5.59E+01 4.92E+01 5.58E+01 53.633 ppm@7%O2 5.08E+01 4.38E+01 4.93E+01 47.967



### Location: Unit 1 - OTM - 27/28 Compound: Filterable PM2.5 Average RunNumber 1 2 3 Mass_mg 3.4 6.9 6.5 5.600 Elb/hr 1.04E+00 2.09E+00 1.98E+00 1.703 gr/dscf 4.11E-04 8.31E-04 7.66E-04 0.001 lb/mmBtuO2 8.25E-04 1.64E-03 1.55E-03 0.001 

### Compound: Inorganic (Aqueous) Condensible Pa Average RunNumber 1 2 3 Mass_mg 80.7 77.9 32.1 63.567 Elb/hr 2.47E+01 2.36E+01 9.76E+00 19.353 gr/dscf 9.74E-03 9.38E-03 3.78E-03 0.008 lb/mmBtuO2 1.96E-02 1.85E-02 7.67E-03 0.015


### Tuesday, March 01, 2011 Page 11 of 22

### Northampton Generating Company, LP EPA MACT

Process Run Data Compound: Organic Condensible Particulate Average RunNumber 1 2 3 Mass_mg 0.7 3.4 0.8 1.633 Elb/hr 2.14E-01 1.03E+00 2.43E-01 0.496 gr/dscf 8.45E-05 4.10E-04 9.42E-05 0.000 lb/mmBtuO2 1.70E-04 8.06E-04 1.91E-04 0.000 

### Compound: Total PM2.5 Average RunNumber 1 2 3 Mass_mg 84.8 88.2 39.4 70.800 Elb/hr 2.59E+01 2.67E+01 1.20E+01 21.533 gr/dscf 1.02E-02 1.06E-02 4.64E-03 0.008 lb/mmBtuO2 2.06E-02 2.09E-02 9.41E-03 0.017



### Tuesday, March 01, 2011 Page 12 of 22

### Northampton Generating Company, LP EPA MACT

Process Run Data

APCD Run Data

Process Lab Run Data 

### Run Name Value UOM Comments Target Value 1 0 /hr


### 1 Total Coal Fow 188100 lb/hr 0
1 Main Steam Temp 1005 Deg. F 0
1 Main Steam Pressure 2395 PSIG 0


### 1 Main Steam Flow 809 lb/hr 0

Run Name Value UOM Comments Target Value 1 DRY LIMESTONE INJECTION 19.7 KLB/Hr 0
1 SELECTIVE NONCATALYTIC REDUCTION FOR NOX 934.5 LB/Hr 0

1 FABRIC FILTER - MEDIUM TEMPERATURE, I.E. 180F<T<25 6.007inches of water 0

Run Name Value UOM Comments 

### 1 Ash content, solid fuel 42.88 % 1 Moisture content, soid fuel 15.26 % 1 Energey content, solid fuel 5884 BTU/lb 1 Sulfur content, solid fuel Sulfur Content, solid fuel 0.28 %

1 Volatile matter content, solid fuel 7.56 % 1 Fixed carbon content, solid fuel 34.68 %



### Tuesday, March 01, 2011 Page 13 of 22

### Northampton Generating Company, LP EPA MACT

Sampling / Stack Data Results Detail



### Location Unit 1 - Method 0011 Average Run Number 1 2 3 Test Date 3/24/2010 3/24/2010 3/24/2010 Run Start Time 1:32:00 PM4:01:00 PM 6:15:00 PM Run Finish Time 3:40:00 PM 6:08:00 PM 8:22:00 PM Net Traversing Points 12 12 12 Net Run Time, minutes 120 120 120 Nozzle Diameter, inches 0.18 0.18 0.18 0.180 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.99 0.97 0.99 0.983 Barometric Pressure, inches of Mercury 29.88 29.88 29.92 29.893 Average Orifice Meter Differential, inches H2O 1.63 1.55 1.74 1.640 Dry Gas Meter Volume Sampled, cubic feet 81.452 92.571 86.169 86.731 Average Dry Gas Meter Temperature, °F 65.83 77.83 76.33 73.330 Dry Gas Meter Volume Sampled, dscf 81.186 88.371 84.341 84.633 Total Moisture Liquid collected, g 126.7 141.2 146.8 138.233 Volume of Water Vapor, standard cubic feet 5.96 6.65 6.91 6.507 Moisture Content of Stack Gas, % 6.84 7.00 7.57 7.137 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9316 0.93 0.9243 0.929 Carbon Dioxide, % 15.35 15.54 15.13 15.340 Oxygen, % 5.34 5.33 5.66 5.443 Carbon Monoxide & Nitrogen, % 79.31 79.13 79.21 79.217 Fuel Factor 1.01 1.00 1.01 Dry Molecular Weight, lb/lb-Mole 30.67 30.70 30.65 30.673 Wet Molecular weight, lb/lb-Mole 29.80 29.81 29.69 29.767 Flue Gas Static Pressure, inches of H2O -2 -2 -2 -2.000 Absolute Flue Gas Pressure, inches of Mercury 29.73 29.73 29.77 29.743 Average Stack Gas Temperature, °F 320.08 326.08 328.33 324.830 Average Velocity Head, inches of H2O 2.4255113344 36722.595401493

59542.511846648

00852 2.511
Average Stack Gas Velocity, feet/second 104.94 108.96 107.49 107.130 Stack Cross-Sectional Area, square feet 70.882 70.882 70.882 70.882 Dry Volumetric Flow Rate, dry scfm 279,631.3 287,632.4 281,586.2282,949.967 Actual Wet Volumetric Flue Gas Flow Rate, acfm 446,301.4 463,398.2 457,146.4455,615.333 Percent Isokinetic of Sampling Rate, % 97.0 102.7 100.1 99.933 Percent Excess Air, % 34.2 34.3 37.1 35.200 F-Factor, dscfm/MMBtu @ %O2 10204 10345 1048310,344.000 Round Duct Diameter, inches 114 114 114 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



### Tuesday, March 01, 2011 Page 14 of 22

### Northampton Generating Company, LP EPA MACT

Location Unit 1 - Method 10 Average Run Number 1 2 3 Test Date 3/24/2010 3/24/2010 3/24/2010 Run Start Time 1:32:00 PM4:01:00 PM 6:15:00 PM Run Finish Time 3:40:00 PM 6:08:00 PM 8:22:00 PM Carbon Dioxide, % 15.35 15.54 15.13 15.340 Oxygen, % 5.34 5.33 5.66 5.443 Fuel Factor 1.01 1 1.01 Dry Volumetric Flow Rate, dry scfm 279523 287529 281473282,841.667 F-Factor, dscfm/MMBtu @ %O2 10204 10345 1048310,344.000 Moisture, % 6.8 7 7.6 7.133 Analyzer Make Thermo Environmental Instruments Thermo

Environment

al Instruments Thermo

Environmenta l Instruments
Analyzer Model 48C 48C 48C Analyzer Serial Number 33560-245 33560-245 33560-245 Operating Range 173.6 173.6 173.6 173.600 Operating Units ppm ppm ppm No. Readings/Avg. 60 60 60 60.000 Calibration Set 7 8 9 8.000 Calibration Pre Zero Cylinder ID ZEROTESTZEROTEST ZEROTEST Calibration Pre Zero Cylinder Instrument Response -1 -1 0 -0.667 Calibration Pre Zero Cylinder Bias 0 0 0.58 0.193 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID SG900969 SG900969 SG900969 Calibration Pre High Cylinder Instrument Response 88.9 87.9 87.9 88.233 Calibration Pre High Cylinder Bias 0 -0.58 -0.58 -0.387 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID ZEROTESTZEROTEST ZEROTEST Calibration Post Zero Cylinder Instrument Response -1 0 0 -0.333 Calibration Post Zero Cylinder Bias 0 0.58 0.58 0.387 Calibration Post Zero Cylinder Drift 0 0.58 0 0.193 Calibration Post High Cylinder ID SG900969 SG900969 SG900969 Calibration Post High Cylinder Instrument Response 87.9 87.9 89.8 88.533 Calibration Post High Cylinder Bias -0.58 -0.58 0.52 -0.213 Calibration Post High Cylinder Drift 0.58 0 1.1 0.560 Cavg 103.8 104.9 109.2 105.967 Cavg Units ppmvd ppmvd ppmvd Cgas 105.3627 107.1646 110.4659 107.664 Cgas Units ppmvd ppmvd ppmvd Fuel Type Override Override Override Fw 0 0 0 0.000 Fc 0 0 0 0.000 Cgasw 0 0 0 0.000 Cgasw Units



### Tuesday, March 01, 2011 Page 15 of 22

### Northampton Generating Company, LP EPA MACT

Location Unit 1 - Method 25A Average Run Number 1 2 3 Test Date 3/24/2010 3/24/2010 3/24/2010 Run Start Time 1:32:00 PM4:01:00 PM 6:15:00 PM Run Finish Time 3:40:00 PM 6:08:00 PM 8:22:00 PM Carbon Dioxide, % 15.35 15.54 15.13 15.340 Oxygen, % 5.34 5.33 5.66 5.443 Fuel Factor 1.01 1 1.01 Dry Volumetric Flow Rate, dry scfm 279523 287529 281473282,841.667 F-Factor, dscfm/MMBtu @ %O2 10204 10345 1048310,344.000 Moisture, % 6.84 7 7.6 7.147 Analyzer Make JUM JUM JUM Analyzer Model VE-7 VE-7 VE-7 Analyzer Serial Number 9491289 9491289 94912899,491,289.0 00 Operating Range 20 20 20 20.000 Operating Units ppm ppm ppm No. Readings/Avg. 60 128 60 82.667 Calibration Set 10 11 12 11.000 Calibration Pre Zero Cylinder ID ZEROTESTZEROTEST ZEROTEST Calibration Pre Zero Cylinder Instrument Response -0.1 0.4 0.5 0.267 Calibration Pre Zero Cylinder Bias 0 2.5 3 1.833 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID XC002368BXC002368B XC002368B Calibration Pre High Cylinder Instrument Response 8.9 8.9 9 8.933 Calibration Pre High Cylinder Bias 0 0 0.5 0.167 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID ZEROTESTZEROTEST ZEROTEST Calibration Post Zero Cylinder Instrument Response 0.4 0.5 0.5 0.467 Calibration Post Zero Cylinder Bias 2.5 3 3 2.833 Calibration Post Zero Cylinder Drift 2.5 0.5 0 1.000 Calibration Post High Cylinder ID XC002368BXC002368B XC002368B Calibration Post High Cylinder Instrument Response 8.9 9 9.1 9.000 Calibration Post High Cylinder Bias 0 0.5 1 0.500 Calibration Post High Cylinder Drift 0 0.5 0.5 0.333 Cavg 0.41 0.53 0.82 0.587 Cavg Units ppmvw ppmvw ppmvw Cgas 0.2902 0.0921 0.3686 0.250 Cgas Units ppmvd ppmvd ppmvd Fuel Type Override Override Override Fw 0 0 0 0.000 Fc 0 0 0 0.000 Cgasw 0.2703702857 142868.563764705 88235E-020.340547368

421053 0.232
Cgasw Units ppmvw ppmvw ppmvw



### Tuesday, March 01, 2011 Page 16 of 22

### Northampton Generating Company, LP EPA MACT

Location Unit 1 - Method 26A Average Run Number 1 2 3 Test Date 3/25/2010 3/25/2010 3/25/2010 Run Start Time 6:55:00 AM10:19:00 AM 1:40:00 PM Run Finish Time 10:00:00 AM 1:25:00 PM 4:45:00 PM Net Traversing Points 12 12 12 Net Run Time, minutes 180 180 180 Nozzle Diameter, inches 0.18 0.18 0.18 0.180 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.99 0.99 0.99 0.990 Barometric Pressure, inches of Mercury 30.02 29.99 30.02 30.010 Average Orifice Meter Differential, inches H2O 1.90 1.75 1.74 1.797 Dry Gas Meter Volume Sampled, cubic feet 132.830 128.600 129.511 130.314 Average Dry Gas Meter Temperature, °F 71.42 81.00 82.58 78.333 Dry Gas Meter Volume Sampled, dscf 131.702 125.080 125.721 127.501 Total Moisture Liquid collected, g 226.3 222.5 231 226.600 Volume of Water Vapor, standard cubic feet 10.65 10.47 10.87 10.663 Moisture Content of Stack Gas, % 7.48 7.72 7.96 7.720 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9252 0.9228 0.9204 0.923 Carbon Dioxide, % 15.33 15.32 15.13 15.260 Oxygen, % 5.61 5.3 5.17 5.360 Carbon Monoxide & Nitrogen, % 79.06 79.38 79.7 79.380 Fuel Factor 1.00 1.02 1.04 Dry Molecular Weight, lb/lb-Mole 30.68 30.66 30.63 30.657 Wet Molecular weight, lb/lb-Mole 29.73 29.68 29.62 29.677 Flue Gas Static Pressure, inches of H2O -2 -2 -2 -2.000 Absolute Flue Gas Pressure, inches of Mercury 29.87 29.84 29.87 29.860 Average Stack Gas Temperature, °F 313.75 317.58 322.92 318.083 Average Velocity Head, inches of H2O 2.7875680806 92362.567828472

824392.545281009

29069 2.634
Average Stack Gas Velocity, feet/second 111.92 107.82 107.77 109.170 Stack Cross-Sectional Area, square feet 70.882 70.882 70.882 70.882 Dry Volumetric Flow Rate, dry scfm 300,011.2 286,563.1 284,021.9290,198.733 Actual Wet Volumetric Flue Gas Flow Rate, acfm 475,986.8 458,549.8 458,337.2464,291.267 Percent Isokinetic of Sampling Rate, % 97.8 97.3 98.6 97.900 Percent Excess Air, % 36.8 33.9 32.6 34.433 F-Factor, dscfm/MMBtu @ %O2 10528 10584 1064010,584.000 Round Duct Diameter, inches 114 114 114 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



### Tuesday, March 01, 2011 Page 17 of 22

### Northampton Generating Company, LP EPA MACT

Location Unit 1 - Method 29 Average Run Number 1 2 3 Test Date 3/23/2010 3/23/2010 3/24/2010 Run Start Time 7:30:00 AM2:32:00 PM 6:40:00 AM Run Finish Time 1:45:00 PM 8:48:00 PM12:50:00 PM Net Traversing Points 12 12 12 Net Run Time, minutes 360 360 360 Nozzle Diameter, inches 0.16 0.16 0.16 0.160 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.99 0.99 0.99 0.990 Barometric Pressure, inches of Mercury 29.57 29.5 29.76 29.610 Average Orifice Meter Differential, inches H2O 1.10 0.97 1.00 1.023 Dry Gas Meter Volume Sampled, cubic feet 206.506 193.269 190.334 196.703 Average Dry Gas Meter Temperature, °F 80.75 73.83 56.33 70.303 Dry Gas Meter Volume Sampled, dscf 197.825 187.041 192.133 192.333 Total Moisture Liquid collected, g 372.7 360.4 308.6 347.233 Volume of Water Vapor, standard cubic feet 17.54 16.96 14.53 16.343 Moisture Content of Stack Gas, % 8.14 8.31 7.03 7.827 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9186 0.9169 0.9297 0.922 Carbon Dioxide, % 14.5 15.3 15.68 15.160 Oxygen, % 5.43 5.4 5.36 5.397 Carbon Monoxide & Nitrogen, % 80.07 79.3 78.96 79.443 Fuel Factor 1.07 1.01 0.99 Dry Molecular Weight, lb/lb-Mole 30.54 30.66 30.72 30.640 Wet Molecular weight, lb/lb-Mole 29.52 29.61 29.83 29.653 Flue Gas Static Pressure, inches of H2O -2 -2 -2 -2.000 Absolute Flue Gas Pressure, inches of Mercury 29.42 29.35 29.61 29.460 Average Stack Gas Temperature, °F 322.83 324.83 307.42 318.360 Average Velocity Head, inches of H2O 2.7073922622 82172.395474745

690772.444038605

52482 2.516
Average Stack Gas Velocity, feet/second 112.18 105.62 104.65 107.483 Stack Cross-Sectional Area, square feet 70.882 70.882 70.882 70.882 Dry Volumetric Flow Rate, dry scfm 290,654.2 271,806.7 281,739.0281,399.967 Actual Wet Volumetric Flue Gas Flow Rate, acfm 477,092.6 449,193.4 445,068.1457,118.033 Percent Isokinetic of Sampling Rate, % 96.0 97.0 96.2 96.400 Percent Excess Air, % 34.6 34.8 34.6 34.667 F-Factor, dscfm/MMBtu @ %O2 10412 10215 1055910,395.333 Round Duct Diameter, inches 114 114 114 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



### Tuesday, March 01, 2011 Page 18 of 22

### Northampton Generating Company, LP EPA MACT

Location Unit 1 - Method 5 Average Run Number 1 2 3 Test Date 3/23/2010 3/23/2010 3/24/2010 Run Start Time 7:30:00 AM2:32:00 PM 6:40:00 AM Run Finish Time 1:45:00 PM 8:48:00 PM12:50:00 PM Net Traversing Points 12 12 12 Net Run Time, minutes 360 360 360 Nozzle Diameter, inches 0.16 0.16 0.16 0.160 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.99 0.99 0.99 0.990 Barometric Pressure, inches of Mercury 29.57 29.5 29.76 29.610 Average Orifice Meter Differential, inches H2O 1.10 0.97 1.00 1.023 Dry Gas Meter Volume Sampled, cubic feet 206.506 193.269 190.334 196.703 Average Dry Gas Meter Temperature, °F 80.75 73.83 56.33 70.303 Dry Gas Meter Volume Sampled, dscf 197.825 187.041 192.133 192.333 Total Moisture Liquid collected, g 372.7 360.4 308.6 347.233 Volume of Water Vapor, standard cubic feet 17.54 16.96 14.53 16.343 Moisture Content of Stack Gas, % 8.14 8.31 7.03 7.827 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9186 0.9169 0.9297 0.922 Carbon Dioxide, % 14.5 15.3 15.68 15.160 Oxygen, % 5.43 5.4 5.36 5.397 Carbon Monoxide & Nitrogen, % 80.07 79.3 78.96 79.443 Fuel Factor 1.07 1.01 0.99 Dry Molecular Weight, lb/lb-Mole 30.54 30.66 30.72 30.640 Wet Molecular weight, lb/lb-Mole 29.52 29.61 29.83 29.653 Flue Gas Static Pressure, inches of H2O -2 -2 -2 -2.000 Absolute Flue Gas Pressure, inches of Mercury 29.42 29.35 29.61 29.460 Average Stack Gas Temperature, °F 322.83 324.75 307.42 318.333 Average Velocity Head, inches of H2O 2.7073922622 82172.395474745

690772.444038605

52482 2.516
Average Stack Gas Velocity, feet/second 112.18 105.62 104.65 107.483 Stack Cross-Sectional Area, square feet 70.882 70.882 70.882 70.882 Dry Volumetric Flow Rate, dry scfm 290,654.2 271,834.4 281,739.0281,409.200 Actual Wet Volumetric Flue Gas Flow Rate, acfm 477,092.6 449,193.4 445,068.1457,118.033 Percent Isokinetic of Sampling Rate, % 96.0 97.0 96.2 96.400 Percent Excess Air, % 34.6 34.8 34.6 34.667 F-Factor, dscfm/MMBtu @ %O2 10412 10215 1055910,395.333 Round Duct Diameter, inches 114 114 114 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



### Tuesday, March 01, 2011 Page 19 of 22

### Northampton Generating Company, LP EPA MACT

Location Unit 1 - Method 6C Average Run Number 1 2 3 Test Date 3/25/2010 3/25/2010 3/25/2010 Run Start Time 10:19:00 AM10:19:00 AM 1:40:00 PM Run Finish Time 1:25:00 PM 1:25:00 PM 4:45:00 PM Carbon Dioxide, % 15.33 15.32 15.13 15.260 Oxygen, % 5.61 5.3 5.17 5.360 Fuel Factor 1 1.02 1.04 Dry Volumetric Flow Rate, dry scfm 299903 286451 284905290,419.667 F-Factor, dscfm/MMBtu @ %O2 10528 10584 1064010,584.000 Moisture, % 7.5 7.7 8 7.733 Analyzer Make Bover Analytical Instruments Bover

Analytical Instruments Bover

Analytical Instruments Analyzer Model 721-M 721-M 721-M Analyzer Serial Number 94-721MB193-1 94-721MB193-1 94-721MB193-1 Operating Range 89.9 89.9 89.9 89.900 Operating Units ppm ppm ppm No. Readings/Avg. 60 60 60 60.000 Calibration Set 4 5 6 5.000 Calibration Pre Zero Cylinder ID ZEROTESTZEROTEST ZEROTEST Calibration Pre Zero Cylinder Instrument Response 1.5 2 1.5 1.667 Calibration Pre Zero Cylinder Bias 0 0.56 0 0.187 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID CC 130664 CC 130664 CC 130664 Calibration Pre High Cylinder Instrument Response 47.5 46.9 49.8 48.067 Calibration Pre High Cylinder Bias 0 -0.67 2.56 0.630 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID ZEROTESTZEROTEST ZEROTEST Calibration Post Zero Cylinder Instrument Response 2 1.5 1.5 1.667 Calibration Post Zero Cylinder Bias 0.56 0 0 0.187 Calibration Post Zero Cylinder Drift 0.56 0.56 0 0.373 Calibration Post High Cylinder ID CC 130664 CC 130664 CC 130664 Calibration Post High Cylinder Instrument Response 46.9 49.8 48.3 48.333 Calibration Post High Cylinder Bias -0.67 2.56 0.89 0.927 Calibration Post High Cylinder Drift 0.67 3.23 1.67 1.857 Cavg 48.2 50.8 56.1 51.700 Cavg Units ppmvd ppmvd ppmvd Cgas 49.6693 51.1552 55.8057 52.210 Cgas Units ppmvd ppmvd ppmvd Fuel Type Override Override Override Fw 0 0 0.000 Fc 1800 0 0 600.000 Cgasw 0 0 0 0.000 Cgasw Units



### Tuesday, March 01, 2011 Page 20 of 22

### Northampton Generating Company, LP EPA MACT

Location Unit 1 - Method 7E Average Run Number 1 2 3 Test Date 3/25/2010 3/25/2010 3/25/2010 Run Start Time 6:55:00 AM10:19:00 AM 1:40:00 PM Run Finish Time 10:00:00 AM 1:25:00 PM 4:45:00 PM Carbon Dioxide, % 15.33 15.32 15.13 15.260 Oxygen, % 5.61 5.3 5.17 5.360 Fuel Factor 1 1.02 1.04 Dry Volumetric Flow Rate, dry scfm 299903 286451 284905290,419.667 F-Factor, dscfm/MMBtu @ %O2 10528 10584 1064010,584.000 Moisture, % 7.5 7.7 8 7.733 Analyzer Make Termo Electron Intruments Termo

Electron Intruments Termo

Electron Intruments Analyzer Model 10AR 10AR 10AR Analyzer Serial Number 13608-156 13608-156 1360-156 Operating Range 88.42 88.42 88.42 88.420 Operating Units ppm ppm ppm No. Readings/Avg. 60 60 60 60.000 Calibration Set 1 2 3 2.000 Calibration Pre Zero Cylinder ID ZEROTESTZEROTEST ZEROTEST Calibration Pre Zero Cylinder Instrument Response -0.2 2.1 2.1 1.333 Calibration Pre Zero Cylinder Bias 0.68 3.28 3.28 2.413 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID CC48438 CC48438 CC48438 Calibration Pre High Cylinder Instrument Response 44.7 45.5 45.4 45.200 Calibration Pre High Cylinder Bias -0.68 0.23 0.11 -0.113 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID ZEROTESTZEROTEST ZEROTEST Calibration Post Zero Cylinder Instrument Response 2.1 2.1 2.1 2.100 Calibration Post Zero Cylinder Bias 3.28 3.28 3.28 3.280 Calibration Post Zero Cylinder Drift 2.6 0 0 0.867 Calibration Post High Cylinder ID CC48438 CC48438 CC48438 Calibration Post High Cylinder Instrument Response 45.5 45.4 45.7 45.533 Calibration Post High Cylinder Bias 0.23 0.11 0.45 0.263 Calibration Post High Cylinder Drift 0.91 0.12 0.34 0.457 Cavg 55.2 49 55.4 53.200 Cavg Units ppmvd ppmvd ppmvd Cgas 55.872 49.1936 55.7779 53.615 Cgas Units ppmvd ppmvd ppmvd Fuel Type Override Override Override Fw 0 0 0 0.000 Fc 0 0 0 0.000 Cgasw 0 0 0 0.000 Cgasw Units



### Tuesday, March 01, 2011 Page 21 of 22

### Northampton Generating Company, LP EPA MACT

Location Unit 1 - OTM - 27/28 Average Run Number 1 2 3 Test Date 3/23/2010 3/23/2010 3/24/2010 Run Start Time 7:30:00 AM2:32:00 PM 6:40:00 AM Run Finish Time 1:44:00 PM 8:45:00 PM12:50:00 PM Net Traversing Points 12 12 12 Net Run Time, minutes 358.9 358.4 360 Nozzle Diameter, inches 0.125 0.125 0.125 0.125 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.97 0.97 0.97 0.970 Barometric Pressure, inches of Mercury 29.57 29.5 29.76 29.610 Average Orifice Meter Differential, inches H2O 0.37 0.37 0.37 0.370 Dry Gas Meter Volume Sampled, cubic feet 134.337 135.988 133.159 134.495 Average Dry Gas Meter Temperature, °F 72.50 76.50 58.17 69.057 Dry Gas Meter Volume Sampled, dscf 127.812 128.114 131.030 128.985 Total Moisture Liquid collected, g 233.4 241.5 201.4 225.433 Volume of Water Vapor, standard cubic feet 10.99 11.37 9.48 10.613 Moisture Content of Stack Gas, % 7.92 8.15 6.75 7.607 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9208 0.9185 0.9325 0.924 Carbon Dioxide, % 14.5 15.3 15.68 15.160 Oxygen, % 5.43 5.4 5.36 5.397 Carbon Monoxide & Nitrogen, % 80.07 79.3 78.96 79.443 Fuel Factor 1.07 1.01 0.99 Dry Molecular Weight, lb/lb-Mole 30.54 30.66 30.72 30.640 Wet Molecular weight, lb/lb-Mole 29.55 29.63 29.86 29.680 Flue Gas Static Pressure, inches of H2O -2 -2 -2 -2.000 Absolute Flue Gas Pressure, inches of Mercury 29.42 29.35 29.61 29.460 Average Stack Gas Temperature, °F 320.08 322.75 312.17 318.333 Average Velocity Head, inches of H2O 2.7810940184 82172.772123569

400762.798186573

49097 2.784
Average Stack Gas Velocity, feet/second 113.44 113.43 112.26 113.043 Stack Cross-Sectional Area, square feet 70.882 70.882 70.882 70.882 Dry Volumetric Flow Rate, dry scfm 295,661.4 293,191.7 301,272.1296,708.400 Actual Wet Volumetric Flue Gas Flow Rate, acfm 482,451.2 482,408.7 477,432.8480,764.233 Percent Isokinetic of Sampling Rate, % 100.2 101.4 100.5 100.700 Percent Excess Air, % 34.8 34.6 F-Factor, dscfm/MMBtu @ %O2 10412 10215 1055910,395.333 Round Duct Diameter, inches 114 114 114 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



### Tuesday, March 01, 2011 Page 22 of 22