Name: Richard Carter

Title: Plant Manager

Company: Sunnyside Cogeneration Associates

Sign Date: 9/7/2010

Name: Chet Gutwein

Title: Engineer

Company: Airtech Environmental Services Inc.

Sign Date: 9/7/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Sunnyside Cogeneration Associates Unit 1

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.

Friday, February 18, 2011 Page 1 of 31
Sunnyside Cogeneration Associates Unit 1

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Facility Information:

Sunnyside Cogeneration Associates

1 Power Plant Road

Sunnyside UT 84539

Contact: Rusty Netz

Phone: (435)888-4476 ext. 107

Fax:

Email: rusnetz@hotmail.com

Testing Company:

Airtech Environmental Services Inc.

5776 Lamar Street

Arvada CO 80002

Contact:Jeff Johnson

Phone: (303) 670-0530

Fax: (303) 670-4130

Email: jjohnson@airtechenv.com

Air Permit Number:

50951

Permitted Source ID/Name:

1 Unit 1

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:

The Sunnyside Cogeneration Facility is a steam-electric generating power plant located in Sunnyside, Carbon 

County, Utah (approximately 25 miles southeast of Price). The plant consists of a circulating fluidized bed 

combustion boiler, an emergency backup diesel fire pump, diesel storage tanks, coal handling equipment, ash 

handling equipment, and limestone handling equipment. The boiler is fueled by coal refuse from the Sunnyside and 

Star Point Refuse Piles. The fly/bottom ash generated from the coal combustion is disposed of in an on site landfill 

and/or for beneficial use. Sunnyside is classified as a major source of air pollution with respect to PM10, sulfur 

dioxide (SO2), nitrogen oxide (NOx) and carbon monoxide (CO) emissions. Sunnyside is subject to 40 CFR 64 and 

40 CFR 60, Subpart A, Subpart Kb (40 CFR 60.116b (a) and (b)), Subpart Db (40 CFR 60.40b), and Subpart Y (40 

CFR 60.250).

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 4900700030 FRS #: 110000470008

SCC / Description 10100202 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 102 0 0 102 8 2 3 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Exit % H2O Method 1 - 4 3 180 0

Stack Exit Carbon Monoxide Method 10 3 120 0

Friday, February 18, 2011 Page 2 of 31
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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.

The following is a list of the test methods that are to be used for this test program and their respective promulgation 

dates:

Methods 1 through 29 – August 1997

Method 30B – January 2008

Other Test Methods 27 and 28 – April 2009

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 3 120 0

Stack Exit Chlorine Method 26A 3 180 0

Stack Exit Hydrogen Chloride Method 26A 3 180 0

Stack Exit Hydrogen Fluoride Method 26A 3 180 0

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

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Inorganic (Aqueous) 

Condensible Part.

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Total 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

Stack Exit Phosphorus (yellow or white) Method 29 3 240 0

Stack Exit Antimony Method 29 3 240 0

Stack Exit Arsenic Method 29 3 240 0

Stack Exit Beryllium Method 29 3 240 0

Stack Exit Cadmium Method 29 3 240 0

Stack Exit Chromium Method 29 3 240 0

Stack Exit Lead Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Filterable Particulate Method 29 3 240 0

Stack Exit Cobalt Method 29 3 240 0

Stack Exit Selenium Method 29 3 240 0

Stack Exit O2 Method 3A O2 3 240 0

Stack Exit Co2 Method 3A CO2 3 240 0

Stack Exit Co2 Method 3A CO2 3 120 0

Stack Exit O2 Method 3A O2 3 120 0

Stack Exit O2 Method 3A O2 3 480 0

Stack Exit Co2 Method 3A CO2 3 480 0

Stack Exit Sulfur Dioxide Method 6C 3 180 0

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

Friday, February 18, 2011 Page 3 of 31
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Sampling / Stack Data Results Summary

Location Stack Exit - Method 1 - 4

Average

Run Number 1 2 3

Test Date 6/22/2010 6/22/2010 6/22/2010

Run Start Time 10:25:00 AM 1:12:00 PM 3:52:00 PM

Run Finish Time 12:37:00 PM 3:30:00 PM 6:02:00 PM

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 63.625 63.150 59.717 62.164

Moisture Content of Stack Gas, % 11.80 10.27 10.92 10.997

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

Carbon Dioxide, % 15 14.7 14.9 14.867

Oxygen, % 4.68 4.68 4.6 4.653

Average Stack Gas Temperature, °F 313.08 312.75 313.42 313.083

Dry Volumetric Flow Rate, dry scfm 146,051.3 145,955.0 145,365.8 145,790.700

Actual Wet Volumetric Flue Gas Flow Rate, acfm 304,414.2 298,898.6 300,124.3 301,145.700

Percent Isokinetic of Sampling Rate, % 104.6 103.9 98.7 102.400

F-Factor, dscfm/MMBtu @ %O2 10355 10355 10355 10,355.000

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Stack Exit - Method 10

Average

Run Number NDF1 NDF2 NDF3

Test Date 6/22/2010 6/22/2010 6/22/2010

Run Start Time 11:57:00 AM 1:44:00 PM 3:56:00 PM

Run Finish Time 1:27:00 PM 3:07:00 PM 5:50:00 PM

Carbon Dioxide, % 14.7 14.7 14.9 14.767

Oxygen, % 4.68 4.68 4.6 4.653

Dry Volumetric Flow Rate, dry scfm 146100 145900 145300 145,766.667

F-Factor, dscfm/MMBtu @ %O2 10355 10355 10355 10,355.000

Moisture, % 11.8 10.3 11 11.033

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Friday, February 18, 2011 Page 4 of 31
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Location Stack Exit - Method 25A

Average

Run Number NDF1 NDF2 NDF3

Test Date 6/22/2010 6/22/2010 6/22/2010

Run Start Time 11:57:00 AM 1:44:00 PM 3:56:00 PM

Run Finish Time 1:27:00 PM 3:07:00 PM 5:50:00 PM

Carbon Dioxide, % 14.7 14.7 14.9 14.767

Oxygen, % 4.68 4.68 4.6 4.653

Dry Volumetric Flow Rate, dry scfm 146100 145900 145300 145,766.667

F-Factor, dscfm/MMBtu @ %O2 10355 10355 10355 10,355.000

Moisture, % 11.8 10.3 11 11.033

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Stack Exit - Method 26A

Average

Run Number 1 2 3

Test Date 6/21/2010 6/22/2010 6/22/2010

Run Start Time 1:09:00 PM 10:25:00 

AM

1:53:00 PM

Run Finish Time 4:32:00 PM 1:40:00 PM 5:08:00 PM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 106.158 102.498 101.322 103.326

Moisture Content of Stack Gas, % 10.46 11.78 11.56 11.267

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

Carbon Dioxide, % 13.7 15 14.8 14.500

Oxygen, % 5.4 4.4 4.6 4.800

Average Stack Gas Temperature, °F 315.17 312.67 313.83 313.890

Dry Volumetric Flow Rate, dry scfm 159,596.2 152,684.6 149,497.7 153,926.167

Actual Wet Volumetric Flue Gas Flow Rate, acfm 328,553.6 317,999.0 311,053.4 319,202.000

Percent Isokinetic of Sampling Rate, % 106.5 107.5 108.5 107.500

F-Factor, dscfm/MMBtu @ %O2 10284 10355 10355 10,331.333

Fw 0 0 0 0.000

Fc 0 0 0 0.000

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Location Stack Exit - Method 29

Average

Run Number 1 2 3

Test Date 6/21/2010 6/23/2010 6/24/2010

Run Start Time 1:11:00 AM 9:55:00 

AM

8:00:00 AM

Run Finish Time 5:35:00 PM 2:15:00 PM 12:38:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 127.407 132.376 135.283 131.689

Moisture Content of Stack Gas, % 8.85 11.92 11.55 10.773

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

Carbon Dioxide, % 15.3 15.6 14.9 15.267

Oxygen, % 4.3 4.3 4.52 4.373

Average Stack Gas Temperature, °F 314.58 315.58 314.67 314.943

Dry Volumetric Flow Rate, dry scfm 151,975.0 153,435.2 152,346.5 152,585.567

Actual Wet Volumetric Flue Gas Flow Rate, acfm 307,103.9 322,765.6 320,109.9 316,659.800

Percent Isokinetic of Sampling Rate, % 100.7 103.6 106.6 103.633

F-Factor, dscfm/MMBtu @ %O2 10284 10233 10308 10,275.000

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Stack Exit - Method 3A CO2

Average

Run Number A1 A2 A3

Test Date 6/21/2010 6/22/2010 6/22/2010

Run Start Time 12:48:00 PM 10:02:00 

AM

2:47:00 PM

Run Finish Time 4:13:00 PM 2:36:00 PM 5:50:00 PM

Carbon Dioxide, % 13.7 15 14.8 14.500

Oxygen, % 5.4 4.4 4.6 4.800

Dry Volumetric Flow Rate, dry scfm 159590 152671 149447 153,902.667

F-Factor, dscfm/MMBtu @ %O2 10284 10355 10355 10,331.333

Moisture, % 10.5 11.8 11.6 11.300

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Friday, February 18, 2011 Page 6 of 31
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Location Stack Exit - Method 3A CO2 3

Average

Run Number M1 M2 M33

Test Date 6/21/2010 6/23/2010 6/24/2010

Run Start Time 12:48:00 PM 9:36:00 

AM

7:56:00 AM

Run Finish Time 8:36:00 PM 5:17:00 PM 4:01:00 PM

Carbon Dioxide, % 15.3 15.6 14.9 15.267

Oxygen, % 4.26 4.33 4.52 4.370

Dry Volumetric Flow Rate, dry scfm 151955 153009 152310 152,424.667

F-Factor, dscfm/MMBtu @ %O2 10284 10233 10308 10,275.000

Moisture, % 8.87 12.2 11.6 10.890

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Stack Exit - Method 3A CO2 3 6

Average

Run Number NDF1 NDF2 NDF3

Test Date 6/22/2010 6/22/2010 6/22/2010

Run Start Time 11:57:00 AM 1:44:00 PM 3:56:00 PM

Run Finish Time 1:27:00 PM 3:07:00 PM 5:50:00 PM

Carbon Dioxide, % 14.7 14.7 14.9 14.767

Oxygen, % 4.68 4.68 4.6 4.653

Dry Volumetric Flow Rate, dry scfm 146100 145900 145300 145,766.667

F-Factor, dscfm/MMBtu @ %O2 10355 10355 10355 10,355.000

Moisture, % 11.8 10.3 11 11.033

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Friday, February 18, 2011 Page 7 of 31
Sunnyside Cogeneration Associates Unit 1

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Location Stack Exit - Method 3A O2

Average

Run Number A1 A2 A3

Test Date 6/21/2010 6/22/2010 6/22/2010

Run Start Time 12:48:00 PM 10:02:00 

AM

2:47:00 PM

Run Finish Time 4:13:00 PM 2:36:00 PM 5:50:00 PM

Carbon Dioxide, % 13.7 15 14.8 14.500

Oxygen, % 5.4 4.4 4.6 4.800

Dry Volumetric Flow Rate, dry scfm 159590 152671 149447 153,902.667

F-Factor, dscfm/MMBtu @ %O2 10284 10355 10355 10,331.333

Moisture, % 10.5 11.8 11.6 11.300

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Stack Exit - Method 3A O2 3

Average

Run Number M1 M2 M3

Test Date 6/21/2010 6/23/2010 6/24/2010

Run Start Time 12:48:00 PM 9:36:00 

AM

7:56:00 AM

Run Finish Time 8:36:00 PM 5:17:00 PM 4:01:00 PM

Carbon Dioxide, % 15.3 15.6 14.9 15.267

Oxygen, % 4.26 4.33 4.52 4.370

Dry Volumetric Flow Rate, dry scfm 151955 153009 152310 152,424.667

F-Factor, dscfm/MMBtu @ %O2 10284 10233 10308 10,275.000

Moisture, % 8.87 12.2 11.6 10.890

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Friday, February 18, 2011 Page 8 of 31
Sunnyside Cogeneration Associates Unit 1

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Location Stack Exit - Method 3A O2 3 6

Average

Run Number NDF1 NDF2 NDF3

Test Date 6/22/2010 6/22/2010 6/22/2010

Run Start Time 11:57:00 AM 1:44:00 PM 3:56:00 PM

Run Finish Time 1:27:00 PM 3:07:00 PM 5:50:00 PM

Carbon Dioxide, % 14.7 14.7 14.9 14.767

Oxygen, % 4.68 4.68 4.6 4.653

Dry Volumetric Flow Rate, dry scfm 146100 145900 145300 145,766.667

F-Factor, dscfm/MMBtu @ %O2 10355 10355 10355 10,355.000

Moisture, % 11.8 10.3 11 11.033

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Stack Exit - Method 6C

Average

Run Number A1 A2 A3

Test Date 6/21/2010 6/22/2010 6/22/2010

Run Start Time 12:48:00 PM 10:02:00 

AM

2:47:00 PM

Run Finish Time 4:13:00 PM 2:36:00 PM 5:50:00 PM

Carbon Dioxide, % 13.7 15 14.8 14.500

Oxygen, % 5.4 4.4 4.6 4.800

Dry Volumetric Flow Rate, dry scfm 159590 152671 149447 153,902.667

F-Factor, dscfm/MMBtu @ %O2 10284 10355 10355 10,331.333

Moisture, % 10.5 11.8 11.6 11.300

Fuel Type Override Override Override

Fw 0 0 0.000

Fc 0 0 1420 473.333

Friday, February 18, 2011 Page 9 of 31
Sunnyside Cogeneration Associates Unit 1

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Location Stack Exit - Method 7E

Average

Run Number A1 A2 A3

Test Date 6/21/2010 6/22/2010 6/22/2010

Run Start Time 12:48:00 PM 10:02:00 

AM

2:47:00 PM

Run Finish Time 4:13:00 PM 2:36:00 PM 5:50:00 PM

Carbon Dioxide, % 13.7 15 14.8 14.500

Oxygen, % 5.4 4.4 4.6 4.800

Dry Volumetric Flow Rate, dry scfm 159.59 152671 149447 100,759.197

F-Factor, dscfm/MMBtu @ %O2 10284 10355 10355 10,331.333

Moisture, % 10.5 11.8 11.6 11.300

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Stack Exit - OTM - 27/28

Average

Run Number 1 2 3

Test Date 6/21/2010 6/23/2010 6/24/2010

Run Start Time 12:58:00 PM 9:38:00 

AM

8:20:00 AM

Run Finish Time 7:49:00 PM 5:21:00 PM 4:15:00 PM

Net Run Time, minutes 450 450 450

Dry Gas Meter Volume Sampled, dscf 139.233 145.189 141.794 142.072

Moisture Content of Stack Gas, % 8.98 11.62 11.31 10.637

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

Carbon Dioxide, % 15.3 15.6 14.9 15.267

Oxygen, % 4.3 4.3 4.52 4.373

Average Stack Gas Temperature, °F 314.58 315.08 316.17 315.277

Dry Volumetric Flow Rate, dry scfm 159,009.7 149,360.6 153,372.7 153,914.333

Actual Wet Volumetric Flue Gas Flow Rate, acfm 321,778.2 312,926.0 322,016.5 318,906.900

Percent Isokinetic of Sampling Rate, % 96.3 106.9 101.7 101.633

F-Factor, dscfm/MMBtu @ %O2 10284 10233 10308 10,275.000

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Friday, February 18, 2011 Page 10 of 31
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Emissions Summary

Location: Stack Exit - Method 1 - 4

Compound: % H2O

Average

RunNumber 1 2 3

Mass_mg 180700 159600 155600 165,300.000

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run NDF1 NDF2 NDF3

lb/mmBtuO2 3.42E-02 3.18E-02 3.18E-02 0.033

ppm 3.52E+01 3.28E+01 3.30E+01 33.667

ppm@7%O2 3.02E+01 2.81E+01 2.81E+01 28.800

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run NDF1 NDF2 NDF3

lb/mmBtuO2 7.64E-04 7.64E-04 7.60E-04 0.001

ppm 5.00E-01 5.00E-01 5.00E-01 0.500

ppm@7%O2 4.28E-01 4.28E-01 4.26E-01 0.427

Location: Stack Exit - Method 26A

Compound: Chlorine

Average

RunNumber 1 2 3

Mass_mg 52.36 54.245 56.73 54.445

Elb/hr 1.04E+01 1.07E+01 1.11E+01 10.733

lb/mmBtuO2 1.51E-02 1.53E-02 1.64E-02 0.016

mg/dscm 1.74E+01 1.87E+01 1.98E+01 18.633

mg/dscm@7%O2 1.56E+01 1.58E+01 1.69E+01 16.100

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 53.8 55.8 58.3 55.967

Elb/hr 1.07E+01 1.10E+01 1.14E+01 11.033

lb/mmBtuO2 1.55E-02 1.57E-02 1.68E-02 0.016

mg/dscm 1.79E+01 1.92E+01 2.03E+01 19.133

mg/dscm@7%O2 1.61E+01 1.62E+01 1.73E+01 16.533

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.419 0.367 0.399 0.395

Elb/hr 8.33E-02 7.23E-02 7.79E-02 0.078

lb/mmBtuO2 1.21E-04 1.04E-04 1.15E-04 0.000

mg/dscm 1.39E-01 1.26E-01 1.39E-01 0.135

mg/dscm@7%O2 1.25E-01 1.06E-01 1.19E-01 0.117

Friday, February 18, 2011 Page 11 of 31
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Location: Stack Exit - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.000346 0.000229 0.000727 0.000

Elb/hr 5.46E-05 3.51E-05 1.08E-04 0.000

lb/mmBtuO2 7.75E-08 4.91E-08 1.56E-07 0.000

mg/dscm 9.59E-05 6.11E-05 1.90E-04 0.000

mg/dscm@7%O2 8.03E-05 5.12E-05 1.61E-04 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.000425 0.000474 0.000487 0.000

Elb/hr 6.71E-05 7.27E-05 7.25E-05 0.000

lb/mmBtuO2 9.52E-08 1.02E-07 1.04E-07 0.000

mg/dscm 1.18E-04 1.26E-04 1.27E-04 0.000

mg/dscm@7%O2 9.88E-05 1.06E-04 1.08E-04 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.000086 0.00014 0.000115 0.000

Elb/hr 1.36E-05 2.15E-05 1.71E-05 0.000

lb/mmBtuO2 1.93E-08 3.00E-08 2.46E-08 0.000

mg/dscm 2.38E-05 3.74E-05 3.00E-05 0.000

mg/dscm@7%O2 1.99E-05 3.13E-05 2.55E-05 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.0036 0.00555 0.00338 0.004

Elb/hr 5.68E-04 8.51E-04 5.03E-04 0.001

lb/mmBtuO2 8.07E-07 1.19E-06 7.24E-07 0.000

mg/dscm 9.98E-04 1.48E-03 8.82E-04 0.001

mg/dscm@7%O2 8.36E-04 1.24E-03 7.48E-04 0.001

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.00339 0.0145 0.00249 0.007

Elb/hr 5.35E-04 2.22E-03 3.71E-04 0.001

lb/mmBtuO2 7.60E-07 3.11E-06 5.34E-07 0.000

mg/dscm 9.40E-04 3.87E-03 6.50E-04 0.002

mg/dscm@7%O2 7.87E-04 3.24E-03 5.52E-04 0.002

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.000334 0.000531 0.000394 0.000

Elb/hr 5.27E-05 8.14E-05 5.87E-05 0.000

lb/mmBtuO2 7.48E-08 1.14E-07 8.44E-08 0.000

mg/dscm 9.26E-05 1.42E-04 1.03E-04 0.000

Friday, February 18, 2011 Page 12 of 31
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mg/dscm@7%O2 7.75E-05 1.19E-04 8.74E-05 0.000

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 16.6 21.4 26 21.333

Elb/hr 2.62E+00 3.28E+00 3.87E+00 3.257

lb/mmBtuO2 3.72E-03 4.59E-03 5.57E-03 0.005

mg/dscm 4.60E+00 5.71E+00 6.79E+00 5.700

mg/dscm@7%O2 3.85E+00 4.78E+00 5.76E+00 4.797

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.00173 0.00132 0.00131 0.001

Elb/hr 2.73E-04 2.02E-04 1.95E-04 0.000

lb/mmBtuO2 3.88E-07 2.83E-07 2.81E-07 0.000

mg/dscm 4.80E-04 3.52E-04 3.42E-04 0.000

mg/dscm@7%O2 4.02E-04 2.95E-04 2.90E-04 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.00313 0.00509 0.00352 0.004

Elb/hr 4.94E-04 7.80E-04 5.24E-04 0.001

lb/mmBtuO2 7.01E-07 1.09E-06 7.54E-07 0.000

mg/dscm 8.68E-04 1.36E-03 9.19E-04 0.001

mg/dscm@7%O2 7.27E-04 1.14E-03 7.80E-04 0.001

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.00175 0.00371 0.00224 0.003

Elb/hr 2.76E-04 5.69E-04 3.34E-04 0.000

lb/mmBtuO2 3.92E-07 7.96E-07 4.80E-07 0.000

mg/dscm 4.85E-04 9.90E-04 5.85E-04 0.001

mg/dscm@7%O2 4.06E-04 8.29E-04 4.96E-04 0.001

Compound: Phosphorus (yellow or white)

Average

RunNumber 1 2 3

Mass_mg 0.238 0.257 0.24 0.245

Elb/hr 3.76E-02 3.94E-02 3.58E-02 0.038

lb/mmBtuO2 5.33E-05 5.51E-05 5.14E-05 0.000

mg/dscm 6.60E-02 6.86E-02 6.27E-02 0.066

mg/dscm@7%O2 5.53E-02 5.74E-02 5.32E-02 0.055

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.0002 0.000216 0.000229 0.000

Elb/hr 3.16E-05 3.31E-05 3.41E-05 0.000

lb/mmBtuO2 4.48E-08 4.63E-08 4.91E-08 0.000

mg/dscm 5.54E-05 5.76E-05 5.98E-05 0.000

Friday, February 18, 2011 Page 13 of 31
Sunnyside Cogeneration Associates Unit 1

9/7/2010

mg/dscm@7%O2 4.64E-05 4.82E-05 5.07E-05 0.000

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Run A1 A2 A3

Elb/hr 1.22E+02 1.29E+02 1.23E+02 124.667

lb/mmBtuO2 1.77E-01 1.85E-01 1.83E-01 0.182

mg/dscm 2.04E+02 2.26E+02 2.21E+02 217.000

mg/dscm@7%O2 1.83E+02 1.90E+02 1.88E+02 187.000

ppm 7.66E+01 8.48E+01 8.28E+01 81.400

ppm@7%O2 6.87E+01 7.14E+01 7.06E+01 70.233

Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run A1 A2 A3

Elb/hr 1.17E-01 1.23E+02 1.27E+02 83.372

lb/mmBtuO2 1.70E-01 1.77E-01 1.88E-01 0.178

mg/dscm 1.96E+02 2.16E+02 2.27E+02 213.000

mg/dscm@7%O2 1.76E+02 1.82E+02 1.94E+02 184.000

ppm 1.03E+02 1.13E+02 1.19E+02 111.667

ppm@7%O2 9.24E+01 9.52E+01 1.01E+02 96.200

Location: Stack Exit - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 8.9 15.8 12.5 12.400

lb/mmBtuO2 1.82E-03 3.09E-03 2.56E-03 0.002

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 0.2 0 0 0.067

lb/mmBtuO2 4.10E-05 0.00E+00 0.00E+00 0.000

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 6.9 9.1 10.5 8.833

lb/mmBtuO2 1.41E-03 1.78E-03 2.15E-03 0.002

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 4.6 3.5 4.4 4.167

lb/mmBtuO2 9.43E-04 6.85E-04 9.00E-04 0.001

Compound: Total Particulate

Average

RunNumber 1 2 3

Friday, February 18, 2011 Page 14 of 31
Sunnyside Cogeneration Associates Unit 1

9/7/2010

Process Run Data

Mass_mg 20.4 28.4 27.4 25.400

lb/mmBtuO2 4.18E-03 5.56E-03 5.60E-03 0.005

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 11.7 12.6 14.9 13.067

lb/mmBtuO2 2.40E-03 2.46E-03 3.05E-03 0.003

Friday, February 18, 2011 Page 15 of 31
Sunnyside Cogeneration Associates Unit 1

9/7/2010

Process Run Data

APCD Run Data

Run Name Value UOM Comments

Target

Value

1 Coal Firing Rate 51.04 tons/hr 50

2 Coal Firing Rate 49.5 tons/hr 50

3 Coal Firing Rate 49.52 tons/hr 50

4 Coal Firing Rate 51.2 tons/hr 50

1 Average Heat Input 9.014 MMBtu/hr 9

2 Average Heat Input 10.006 MMBtu/hr 9

3 Average Heat Input 11.201 MMBtu/hr 9

4 Average Heat Input 10.883 MMBtu/hr 9

1 Steam Output 460 1000 lb steam/hr 480

2 Steam Output 473.96 1000 lb steam/hr 480

3 Steam Output 475.35 1000 lb steam/hr 480

4 Steam Output 469.98 1000 lb steam/hr 480

1 Flue Gas Oxygen Content 4.45 % 4.5

2 Flue Gas Oxygen Content 4.58 % 4.5

3 Flue Gas Oxygen Content 4.5 % 4.5

4 Flue Gas Oxygen Content 4.48 % 4.5

1 Unit Gross Electrical Output 58 MW 58

2 Unit Gross Electrical Output 58.32 MW 58

3 Unit Gross Electrical Output 58.24 MW 58

4 Unit Gross Electrical Output 58.32 MW 58

1 Unit Net Electric Generation 51.3 MWh 51

2 Unit Net Electric Generation 51.86 MWh 51

3 Unit Net Electric Generation 51.8 MWh 51

4 Unit Net Electric Generation 51.85 MWh 51

1 Sorbent Injection Rate 3.68 tons/hr 4

2 Sorbent Injection Rate 4.21 tons/hr 4

3 Sorbent Injection Rate 4.71 tons/hr 4

4 Sorbent Injection Rate 4.43 tons/hr 4

Run Name Value UOM Comments

Target

Value

1 List all emissions control devices in order of 

process flow. Choose from

0 0

Friday, February 18, 2011 Page 16 of 31
Sunnyside Cogeneration Associates Unit 1

9/7/2010

Process Lab Run Data

1 drop down lists. If not on list add description and 

provide detailed

0 0

1 desription in section 5a. 0 0

Run Name Value UOM Comments

1 See 4b Comments. 0

Friday, February 18, 2011 Page 17 of 31
Sunnyside Cogeneration Associates Unit 1

9/7/2010

Sampling / Stack Data Results Detail

Location Stack Exit - Method 1 - 4

Average

Run Number 1 2 3

Test Date 6/22/2010 6/22/2010 6/22/2010

Run Start Time 10:25:00 AM 1:12:00 PM 3:52:00 PM

Run Finish Time 12:37:00 PM 3:30:00 PM 6:02:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 120 120 120

Nozzle Diameter, inches 0.19 0.19 0.19 0.190

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9888 0.9888 0.9888 0.989

Barometric Pressure, inches of Mercury 23.89 23.89 23.89 23.890

Average Orifice Meter Differential, inches H2O 1.13 1.09 1.09 1.103

Dry Gas Meter Volume Sampled, cubic feet 81.150 82.630 78.300 80.693

Average Dry Gas Meter Temperature, °F 73.54 87.29 88.42 83.083

Dry Gas Meter Volume Sampled, dscf 63.625 63.150 59.717 62.164

Total Moisture Liquid collected, g 180.7 153.6 155.6 163.300

Volume of Water Vapor, standard cubic feet 8.51 7.23 7.32 7.687

Moisture Content of Stack Gas, % 11.80 10.27 10.92 10.997

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

Dry Mole Fraction 0.882 0.8973 0.8908 0.890

Carbon Dioxide, % 15 14.7 14.9 14.867

Oxygen, % 4.68 4.68 4.6 4.653

Carbon Monoxide & Nitrogen, % 80.32 80.62 80.5 80.480

Fuel Factor 1.08 1.10 1.09

Dry Molecular Weight, lb/lb-Mole 30.59 30.54 30.57 30.567

Wet Molecular weight, lb/lb-Mole 29.10 29.25 29.20 29.183

Flue Gas Static Pressure, inches of H2O -0.8 -0.8 -0.8 -0.800

Absolute Flue Gas Pressure, inches of Mercury 23.83 23.83 23.83 23.830

Average Stack Gas Temperature, °F 313.08 312.75 313.42 313.083

Average Velocity Head, inches of H2O 1.3906337263

6487

1.348221166

10666

1.355690518

7627

1.365

Average Stack Gas Velocity, feet/second 89.41 87.79 88.15 88.450

Stack Cross-Sectional Area, square feet 56.745 56.745 56.745 56.745

Dry Volumetric Flow Rate, dry scfm 146,051.3 145,955.0 145,365.8 145,790.700

Actual Wet Volumetric Flue Gas Flow Rate, acfm 304,414.2 298,898.6 300,124.3 301,145.700

Percent Isokinetic of Sampling Rate, % 104.6 103.9 98.7 102.400

Percent Excess Air, % 28.3 28.2 27.6 28.033

F-Factor, dscfm/MMBtu @ %O2 10355 10355 10355 10,355.000

Round Duct Diameter, inches 102 102 102

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

Friday, February 18, 2011 Page 18 of 31
Sunnyside Cogeneration Associates Unit 1

9/7/2010

Location Stack Exit - Method 10

Average

Run Number NDF1 NDF2 NDF3

Test Date 6/22/2010 6/22/2010 6/22/2010

Run Start Time 11:57:00 AM 1:44:00 PM 3:56:00 PM

Run Finish Time 1:27:00 PM 3:07:00 PM 5:50:00 PM

Carbon Dioxide, % 14.7 14.7 14.9 14.767

Oxygen, % 4.68 4.68 4.6 4.653

Fuel Factor 1.1 1.1 1.09

Dry Volumetric Flow Rate, dry scfm 146100 145900 145300 145,766.667

F-Factor, dscfm/MMBtu @ %O2 10355 10355 10355 10,355.000

Moisture, % 11.8 10.3 11 11.033

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 1000 1000 1000 1,000.000

Operating Units ppm ppm ppm

No. Readings/Avg. 60 60 60 60.000

Calibration Set 100 100 100 100.000

Calibration Pre Zero Cylinder ID 00-Zero 00-Zero 00-Zero

Calibration Pre Zero Cylinder Instrument Response 0.3 -0.2 -0.4 -0.100

Calibration Pre Zero Cylinder Bias 0.3 -0.2 -0.39 -0.097

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID XC030124BCOXC030124BCOXC030124BCO

Calibration Pre High Cylinder Instrument Response 48.6 48.3 48 48.300

Calibration Pre High Cylinder Bias -0.39 -0.69 -0.99 -0.690

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID 00-Zero 00-Zero 00-Zero

Calibration Post Zero Cylinder Instrument Response -0.2 -0.4 -0.4 -0.333

Calibration Post Zero Cylinder Bias -0.2 -0.39 -0.39 -0.327

Calibration Post Zero Cylinder Drift 0.5 0.19 0 0.230

Calibration Post High Cylinder ID XC030124BCOXC030124BCOXC030124BCO

Calibration Post High Cylinder Instrument Response 48.3 48 47.6 47.967

Calibration Post High Cylinder Bias -0.69 -0.99 -1.38 -1.020

Calibration Post High Cylinder Drift 0.3 0.3 0.39 0.330

Cavg 34.6 31.9 31.8 32.767

Cavg Units ppmvd ppmvd ppmvd

Cgas 35.2496 32.8181 32.9883 33.685

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

Friday, February 18, 2011 Page 19 of 31
Sunnyside Cogeneration Associates Unit 1

9/7/2010

Location Stack Exit - Method 25A

Average

Run Number NDF1 NDF2 NDF3

Test Date 6/22/2010 6/22/2010 6/22/2010

Run Start Time 11:57:00 AM 1:44:00 PM 3:56:00 PM

Run Finish Time 1:27:00 PM 3:07:00 PM 5:50:00 PM

Carbon Dioxide, % 14.7 14.7 14.9 14.767

Oxygen, % 4.68 4.68 4.6 4.653

Fuel Factor 1.1 1.1 1.09

Dry Volumetric Flow Rate, dry scfm 146100 145900 145300 145,766.667

F-Factor, dscfm/MMBtu @ %O2 10355 10355 10355 10,355.000

Moisture, % 11.8 10.3 11 11.033

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 1000 1000 1000 1,000.000

Operating Units ppm ppm ppm

No. Readings/Avg. 60 60 60 60.000

Calibration Set 25 25 25 25.000

Calibration Pre Zero Cylinder ID 00-Zero 00-Zero 00-Zero

Calibration Pre Zero Cylinder Instrument Response 0 0 0 0.000

Calibration Pre Zero Cylinder Bias -0.3 0 0 -0.100

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC52193-

Propane

CC52193-

Propane

CC52193-

Propane

Calibration Pre High Cylinder Instrument Response 30.15 30.15 30.15 30.150

Calibration Pre High Cylinder Bias 0.65 0 0 0.217

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID 00-Zero 00-Zero 00-Zero

Calibration Post Zero Cylinder Instrument Response 0 0 0 0.000

Calibration Post Zero Cylinder Bias -0.3 0 0 -0.100

Calibration Post Zero Cylinder Drift 0 0 0 0.000

Calibration Post High Cylinder ID CC52193-

Propane

CC52193-

Propane

CC52193-

Propane

Calibration Post High Cylinder Instrument Response 30.15 30.15 30.15 30.150

Calibration Post High Cylinder Bias 0.65 0 0 0.217

Calibration Post High Cylinder Drift 0 0 0 0.000

Cavg 0.5 0.5 0.5 0.500

Cavg Units ppmvd ppmvd ppmvd

Cgas 0.5 0.5 0.5 0.500

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 ppmvw

Friday, February 18, 2011 Page 20 of 31
Sunnyside Cogeneration Associates Unit 1

9/7/2010

Location Stack Exit - Method 26A

Average

Run Number 1 2 3

Test Date 6/21/2010 6/22/2010 6/22/2010

Run Start Time 1:09:00 PM 10:25:00 AM 1:53:00 PM

Run Finish Time 4:32:00 PM 1:40:00 PM 5:08:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 180 180 180

Nozzle Diameter, inches 0.19 0.19 0.19 0.190

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.0163 1.0163 1.0163 1.016

Barometric Pressure, inches of Mercury 23.89 23.89 23.89 23.890

Average Orifice Meter Differential, inches H2O 1.32 1.27 1.21 1.267

Dry Gas Meter Volume Sampled, cubic feet 135.340 128.600 129.640 131.193

Average Dry Gas Meter Temperature, °F 88.46 79.67 90.25 86.127

Dry Gas Meter Volume Sampled, dscf 106.158 102.498 101.322 103.326

Total Moisture Liquid collected, g 263.4 290.6 281.6 278.533

Volume of Water Vapor, standard cubic feet 12.40 13.68 13.25 13.110

Moisture Content of Stack Gas, % 10.46 11.78 11.56 11.267

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

Dry Mole Fraction 0.8954 0.8822 0.8844 0.887

Carbon Dioxide, % 13.7 15 14.8 14.500

Oxygen, % 5.4 4.4 4.6 4.800

Carbon Monoxide & Nitrogen, % 80.9 80.6 80.6 80.700

Fuel Factor 1.13 1.10 1.10

Dry Molecular Weight, lb/lb-Mole 30.41 30.58 30.55 30.513

Wet Molecular weight, lb/lb-Mole 29.11 29.10 29.10 29.103

Flue Gas Static Pressure, inches of H2O -0.8 -0.8 -0.8 -0.800

Absolute Flue Gas Pressure, inches of Mercury 23.83 23.83 23.83 23.830

Average Stack Gas Temperature, °F 315.17 312.67 313.83 313.890

Average Velocity Head, inches of H2O 1.6159320778

592

1.518264484

21529

1.450410579

15667

1.528

Average Stack Gas Velocity, feet/second 96.50 93.40 91.36 93.753

Stack Cross-Sectional Area, square feet 56.745 56.745 56.745 56.745

Dry Volumetric Flow Rate, dry scfm 159,596.2 152,684.6 149,497.7 153,926.167

Actual Wet Volumetric Flue Gas Flow Rate, acfm 328,553.6 317,999.0 311,053.4 319,202.000

Percent Isokinetic of Sampling Rate, % 106.5 107.5 108.5 107.500

Percent Excess Air, % 33.8 26.1 27.6 29.167

F-Factor, dscfm/MMBtu @ %O2 10284 10355 10355 10,331.333

Round Duct Diameter, inches 102 102 102

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

Friday, February 18, 2011 Page 21 of 31
Sunnyside Cogeneration Associates Unit 1

9/7/2010

Location Stack Exit - Method 29

Average

Run Number 1 2 3

Test Date 6/21/2010 6/23/2010 6/24/2010

Run Start Time 1:11:00 AM 9:55:00 AM 8:00:00 AM

Run Finish Time 5:35:00 PM 2:15:00 PM 12:38:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.19 0.19 0.19 0.190

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9888 1.0163 1.0163 1.007

Barometric Pressure, inches of Mercury 23.89 23.78 23.68 23.783

Average Orifice Meter Differential, inches H2O 1.13 1.28 1.25 1.220

Dry Gas Meter Volume Sampled, cubic feet 164.660 168.030 171.770 168.153

Average Dry Gas Meter Temperature, °F 80.63 83.50 81.33 81.820

Dry Gas Meter Volume Sampled, dscf 127.407 132.376 135.283 131.689

Total Moisture Liquid collected, g 262.9 380.5 375.3 339.567

Volume of Water Vapor, standard cubic feet 12.37 17.91 17.67 15.983

Moisture Content of Stack Gas, % 8.85 11.92 11.55 10.773

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

Dry Mole Fraction 0.9115 0.8808 0.8845 0.892

Carbon Dioxide, % 15.3 15.6 14.9 15.267

Oxygen, % 4.3 4.3 4.52 4.373

Carbon Monoxide & Nitrogen, % 80.4 80.1 80.58 80.360

Fuel Factor 1.08 1.06 1.10

Dry Molecular Weight, lb/lb-Mole 30.62 30.67 30.56 30.617

Wet Molecular weight, lb/lb-Mole 29.50 29.16 29.11 29.257

Flue Gas Static Pressure, inches of H2O -0.8 -0.8 -0.8 -0.800

Absolute Flue Gas Pressure, inches of Mercury 23.83 23.72 23.62 23.723

Average Stack Gas Temperature, °F 314.58 315.58 314.67 314.943

Average Velocity Head, inches of H2O 1.4317440019

4529

1.554327040

78097

1.521293974

38933

1.502

Average Stack Gas Velocity, feet/second 90.20 94.80 94.02 93.007

Stack Cross-Sectional Area, square feet 56.745 56.745 56.745 56.745

Dry Volumetric Flow Rate, dry scfm 151,975.0 153,435.2 152,346.5 152,585.567

Actual Wet Volumetric Flue Gas Flow Rate, acfm 307,103.9 322,765.6 320,109.9 316,659.800

Percent Isokinetic of Sampling Rate, % 100.7 103.6 106.6 103.633

Percent Excess Air, % 25.4 25.5 27.0 25.967

F-Factor, dscfm/MMBtu @ %O2 10284 10233 10308 10,275.000

Round Duct Diameter, inches 102 102 102

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

Friday, February 18, 2011 Page 22 of 31
Sunnyside Cogeneration Associates Unit 1

9/7/2010

Location Stack Exit - Method 3A CO2

Average

Run Number A1 A2 A3

Test Date 6/21/2010 6/22/2010 6/22/2010

Run Start Time 12:48:00 PM 10:02:00 AM 2:47:00 PM

Run Finish Time 4:13:00 PM 2:36:00 PM 5:50:00 PM

Carbon Dioxide, % 13.7 15 14.8 14.500

Oxygen, % 5.4 4.4 4.6 4.800

Fuel Factor 1.13 1.1 1.1

Dry Volumetric Flow Rate, dry scfm 159590 152671 149447 153,902.667

F-Factor, dscfm/MMBtu @ %O2 10284 10355 10355 10,331.333

Moisture, % 10.5 11.8 11.6 11.300

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 25 25 25 25.000

Operating Units % % %

No. Readings/Avg. 60 60 60 60.000

Calibration Set 30 31 31 30.667

Calibration Pre Zero Cylinder ID 00-Zero 00-Zero 00-Zero

Calibration Pre Zero Cylinder Instrument Response 0 0.5 0.5 0.333

Calibration Pre Zero Cylinder Bias 0 4.3 4.3 2.867

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC152301-

CO2

CC152301-

CO2

CC152301-

CO2

Calibration Pre High Cylinder Instrument Response 14 13.8 13.9 13.900

Calibration Pre High Cylinder Bias 1.22 0.22 0.93 0.790

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID 00-Zero 00-Zero 00-Zero

Calibration Post Zero Cylinder Instrument Response -0.4 0.5 0.4 0.167

Calibration Post Zero Cylinder Bias -2.87 4.3 3.58 1.670

Calibration Post Zero Cylinder Drift 2.87 0 0.72 1.197

Calibration Post High Cylinder ID CC152301-

CO2

CC152301-

CO2

CC152301-

CO2

Calibration Post High Cylinder Instrument Response 14 13.9 14 13.967

Calibration Post High Cylinder Bias 1.22 0.93 1.65 1.267

Calibration Post High Cylinder Drift 0 0.71 0.72 0.477

Cavg 13.7 14.9 14.8 14.467

Cavg Units %vd %vd %vd

Cgas 13.6553 15.0472 14.8283 14.510

Cgas Units %vd %vd %vd

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

Friday, February 18, 2011 Page 23 of 31
Sunnyside Cogeneration Associates Unit 1

9/7/2010

Location Stack Exit - Method 3A CO2 3

Average

Run Number M1 M2 M33

Test Date 6/21/2010 6/23/2010 6/24/2010

Run Start Time 12:48:00 PM 9:36:00 AM 7:56:00 AM

Run Finish Time 8:36:00 PM 5:17:00 PM 4:01:00 PM

Carbon Dioxide, % 15.3 15.6 14.9 15.267

Oxygen, % 4.26 4.33 4.52 4.370

Fuel Factor 1.09 1.06 1.1

Dry Volumetric Flow Rate, dry scfm 151955 153009 152310 152,424.667

F-Factor, dscfm/MMBtu @ %O2 10284 10233 10308 10,275.000

Moisture, % 8.87 12.2 11.6 10.890

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 25 25 25 25.000

Operating Units % % %

No. Readings/Avg. 60 60 60 60.000

Calibration Set 30 32 33 31.667

Calibration Pre Zero Cylinder ID 00-Zero 00-Zero 00-Zero

Calibration Pre Zero Cylinder Instrument Response 0 0 0 0.000

Calibration Pre Zero Cylinder Bias 0 0.72 -0.72 0.000

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC152301-

CO2

CC152301-

CO2

CC152301-

CO2

Calibration Pre High Cylinder Instrument Response 13.6 14 14 13.867

Calibration Pre High Cylinder Bias -1.65 0.72 0 -0.310

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID 00-Zero 00-Zero 00-Zero

Calibration Post Zero Cylinder Instrument Response -0.5 0.2 0 -0.100

Calibration Post Zero Cylinder Bias -3.58 2.15 -0.72 -0.717

Calibration Post Zero Cylinder Drift 3.58 1.43 0 1.670

Calibration Post High Cylinder ID CC152301-

CO2

CC152301-

CO2

CC152301-

CO2

Calibration Post High Cylinder Instrument Response 13.3 13.8 14 13.700

Calibration Post High Cylinder Bias -3.8 -0.72 0 -1.507

Calibration Post High Cylinder Drift 2.15 1.44 0 1.197

Cavg 14.7 15.2 14.8 14.900

Cavg Units %vd %vd %vd

Cgas 15.2228 15.2641 14.7471 15.078

Cgas Units %vd %vd %vd

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

Friday, February 18, 2011 Page 24 of 31
Sunnyside Cogeneration Associates Unit 1

9/7/2010

Location Stack Exit - Method 3A CO2 3 6

Average

Run Number NDF1 NDF2 NDF3

Test Date 6/22/2010 6/22/2010 6/22/2010

Run Start Time 11:57:00 AM 1:44:00 PM 3:56:00 PM

Run Finish Time 1:27:00 PM 3:07:00 PM 5:50:00 PM

Carbon Dioxide, % 14.7 14.7 14.9 14.767

Oxygen, % 4.68 4.68 4.6 4.653

Fuel Factor 1.1 1.1 1.09

Dry Volumetric Flow Rate, dry scfm 146100 145900 145300 145,766.667

F-Factor, dscfm/MMBtu @ %O2 10355 10355 10355 10,355.000

Moisture, % 11.8 10.3 11 11.033

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 25 25 25 25.000

Operating Units % % %

No. Readings/Avg. 60 60 60 60.000

Calibration Set 31 31 31 31.000

Calibration Pre Zero Cylinder ID 00-Zero 00-Zero 00-Zero

Calibration Pre Zero Cylinder Instrument Response 0.5 0.1 0.2 0.267

Calibration Pre Zero Cylinder Bias 4.3 1.43 2.15 2.627

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC152301-

CO2

CC152301-

CO2

CC152301-

CO2

Calibration Pre High Cylinder Instrument Response 13.8 14 13.8 13.867

Calibration Pre High Cylinder Bias 0.22 1.65 0.22 0.697

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID 00-Zero 00-Zero 00-Zero

Calibration Post Zero Cylinder Instrument Response 0.1 0.2 -0.1 0.067

Calibration Post Zero Cylinder Bias 1.43 2.15 0 1.193

Calibration Post Zero Cylinder Drift 2.87 0.72 2.15 1.913

Calibration Post High Cylinder ID CC152301-

CO2

CC152301-

CO2

CC152301-

CO2

Calibration Post High Cylinder Instrument Response 14 13.8 14 13.933

Calibration Post High Cylinder Bias 1.65 0.22 1.65 1.173

Calibration Post High Cylinder Drift 1.43 1.43 1.43 1.430

Cavg 14.9 14.7 14.8 14.800

Cavg Units %vd %vd %vd

Cgas 14.9757 14.7616 14.8565 14.865

Cgas Units %vd %vd %vd

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

Friday, February 18, 2011 Page 25 of 31
Sunnyside Cogeneration Associates Unit 1

9/7/2010

Location Stack Exit - Method 3A O2

Average

Run Number A1 A2 A3

Test Date 6/21/2010 6/22/2010 6/22/2010

Run Start Time 12:48:00 PM 10:02:00 AM 2:47:00 PM

Run Finish Time 4:13:00 PM 2:36:00 PM 5:50:00 PM

Carbon Dioxide, % 13.7 15 14.8 14.500

Oxygen, % 5.4 4.4 4.6 4.800

Fuel Factor 1.13 1.1 1.1

Dry Volumetric Flow Rate, dry scfm 159590 152671 149447 153,902.667

F-Factor, dscfm/MMBtu @ %O2 10284 10355 10355 10,331.333

Moisture, % 10.5 11.8 11.6 11.300

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 25 25 25 25.000

Operating Units % % %

No. Readings/Avg. 60 60 60 60.000

Calibration Set 39 38 38 38.333

Calibration Pre Zero Cylinder ID 00-Zero 00-Zero 00-Zero

Calibration Pre Zero Cylinder Instrument Response -0.1 -0.2 0 -0.100

Calibration Pre Zero Cylinder Bias 1.43 -1.43 0 0.000

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC152301-O2 CC152301-

O2

CC152301-

O2

Calibration Pre High Cylinder Instrument Response 7.1 6.9 7 7.000

Calibration Pre High Cylinder Bias 0 -1.43 -0.72 -0.717

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID 00-Zero 00-Zero 00-Zero

Calibration Post Zero Cylinder Instrument Response 0.3 0 0 0.100

Calibration Post Zero Cylinder Bias 4.29 0 0 1.430

Calibration Post Zero Cylinder Drift 2.86 1.43 0 1.430

Calibration Post High Cylinder ID CC152301-O2 CC152301-

O2

CC152301-

O2

Calibration Post High Cylinder Instrument Response 7 7 7 7.000

Calibration Post High Cylinder Bias -0.72 -0.72 -0.72 -0.720

Calibration Post High Cylinder Drift 0.72 0.71 0 0.477

Cavg 5.4 4.36 4.59 4.783

Cavg Units %vd %vd %vd

Cgas 5.3305 4.422 4.5834 4.779

Cgas Units %vd %vd %vd

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

Friday, February 18, 2011 Page 26 of 31
Sunnyside Cogeneration Associates Unit 1

9/7/2010

Location Stack Exit - Method 3A O2 3

Average

Run Number M1 M2 M3

Test Date 6/21/2010 6/23/2010 6/24/2010

Run Start Time 12:48:00 PM 9:36:00 AM 7:56:00 AM

Run Finish Time 8:36:00 PM 5:17:00 PM 4:01:00 PM

Carbon Dioxide, % 15.3 15.6 14.9 15.267

Oxygen, % 4.26 4.33 4.52 4.370

Fuel Factor 1.09 1.06 1.1

Dry Volumetric Flow Rate, dry scfm 151955 153009 152310 152,424.667

F-Factor, dscfm/MMBtu @ %O2 10284 10233 10308 10,275.000

Moisture, % 8.87 12.2 11.6 10.890

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 25 25 25 25.000

Operating Units % % %

No. Readings/Avg. 60 60 60 60.000

Calibration Set 39 37 36 37.333

Calibration Pre Zero Cylinder ID 00-Zero 00-Zero 00-Zero

Calibration Pre Zero Cylinder Instrument Response -0.1 0.1 -0.1 -0.033

Calibration Pre Zero Cylinder Bias 1.43 0 0 0.477

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC152301-O2 CC152301-

O2

CC152301-

O2

Calibration Pre High Cylinder Instrument Response 7.05 7.01 6.84 6.967

Calibration Pre High Cylinder Bias -0.36 -1.07 -2.15 -1.193

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID 00-Zero 00-Zero 00-Zero

Calibration Post Zero Cylinder Instrument Response 0.3 -0.2 0 0.033

Calibration Post Zero Cylinder Bias 4.29 -2.15 0.72 0.953

Calibration Post Zero Cylinder Drift 2.86 2.15 0.72 1.910

Calibration Post High Cylinder ID CC152301-O2 CC152301-

O2

CC152301-

O2

Calibration Post High Cylinder Instrument Response 7.08 7.03 6.98 7.030

Calibration Post High Cylinder Bias -0.14 -0.93 -1.15 -0.740

Calibration Post High Cylinder Drift 0.22 0.14 1 0.453

Cavg 4.33 4.37 4.49 4.397

Cavg Units %vd %vd %vd

Cgas 4.2452 4.37 4.5596 4.392

Cgas Units %vd %vd %vd

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

Friday, February 18, 2011 Page 27 of 31
Sunnyside Cogeneration Associates Unit 1

9/7/2010

Location Stack Exit - Method 3A O2 3 6

Average

Run Number NDF1 NDF2 NDF3

Test Date 6/22/2010 6/22/2010 6/22/2010

Run Start Time 11:57:00 AM 1:44:00 PM 3:56:00 PM

Run Finish Time 1:27:00 PM 3:07:00 PM 5:50:00 PM

Carbon Dioxide, % 14.7 14.7 14.9 14.767

Oxygen, % 4.68 4.68 4.6 4.653

Fuel Factor 1.1 1.1 1.09

Dry Volumetric Flow Rate, dry scfm 146100 145900 145300 145,766.667

F-Factor, dscfm/MMBtu @ %O2 10355 10355 10355 10,355.000

Moisture, % 11.8 10.3 11 11.033

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 25 25 25 25.000

Operating Units % % %

No. Readings/Avg. 60 60 60 60.000

Calibration Set 38 38 38 38.000

Calibration Pre Zero Cylinder ID 00-Zero 00-Zero 00-Zero

Calibration Pre Zero Cylinder Instrument Response -0.2 0.2 -0.1 -0.033

Calibration Pre Zero Cylinder Bias -1.43 1.43 -0.72 -0.240

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC152301-O2 CC152301-

O2

CC152301-

O2

Calibration Pre High Cylinder Instrument Response 6.86 7.02 7.02 6.967

Calibration Pre High Cylinder Bias -1.72 -0.57 -0.57 -0.953

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID 00-Zero 00-Zero 00-Zero

Calibration Post Zero Cylinder Instrument Response 0.2 -0.1 0 0.033

Calibration Post Zero Cylinder Bias 1.43 -0.72 0 0.237

Calibration Post Zero Cylinder Drift 2.86 2.15 0.72 1.910

Calibration Post High Cylinder ID CC152301-O2 CC152301-

O2

CC152301-

O2

Calibration Post High Cylinder Instrument Response 7.02 7.02 6.98 7.007

Calibration Post High Cylinder Bias -0.57 -0.57 -0.86 -0.667

Calibration Post High Cylinder Drift 1.15 0 0.29 0.480

Cavg 4.65 4.72 4.59 4.653

Cavg Units %vd %vd %vd

Cgas 4.6835 4.6834 4.6005 4.656

Cgas Units %vd %vd %vd

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

Friday, February 18, 2011 Page 28 of 31
Sunnyside Cogeneration Associates Unit 1

9/7/2010

Location Stack Exit - Method 6C

Average

Run Number A1 A2 A3

Test Date 6/21/2010 6/22/2010 6/22/2010

Run Start Time 12:48:00 PM 10:02:00 AM 2:47:00 PM

Run Finish Time 4:13:00 PM 2:36:00 PM 5:50:00 PM

Carbon Dioxide, % 13.7 15 14.8 14.500

Oxygen, % 5.4 4.4 4.6 4.800

Fuel Factor 1.13 1.1 1.1

Dry Volumetric Flow Rate, dry scfm 159590 152671 149447 153,902.667

F-Factor, dscfm/MMBtu @ %O2 10284 10355 10355 10,331.333

Moisture, % 10.5 11.8 11.6 11.300

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 1000 1000 1000 1,000.000

Operating Units ppm ppm ppm

No. Readings/Avg. 60 60 60 60.000

Calibration Set 60 61 61 60.667

Calibration Pre Zero Cylinder ID 00-Zero 00-Zero 00-Zero

Calibration Pre Zero Cylinder Instrument Response 6.6 1.4 1.6 3.200

Calibration Pre Zero Cylinder Bias 1.62 0.29 0.37 0.760

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC154255-

SO2

CC154255-

SO2

CC154255-

SO2

Calibration Pre High Cylinder Instrument Response 166.2 164.1 156.7 162.333

Calibration Pre High Cylinder Bias -0.15 -1.62 -4.35 -2.040

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID 00-Zero 00-Zero 00-Zero

Calibration Post Zero Cylinder Instrument Response 18.7 1.6 1.6 7.300

Calibration Post Zero Cylinder Bias 6.08 0.37 0.37 2.273

Calibration Post Zero Cylinder Drift 4.46 0.08 0 1.513

Calibration Post High Cylinder ID CC154255-

SO2

CC154255-

SO2

CC154255-

SO2

Calibration Post High Cylinder Instrument Response 172.8 156.7 153.6 161.033

Calibration Post High Cylinder Bias 2.29 -4.35 -5.49 -2.517

Calibration Post High Cylinder Drift 2.44 2.73 1.14 2.103

Cavg 84.9 82.5 78 81.800

Cavg Units ppmvd ppmvd ppmvd

Cgas 76.649 84.8232 82.7936 81.422

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 0 0 0.000

Fc 0 0 1420 473.333

Cgasw 0 0 0 0.000

Cgasw Units

Friday, February 18, 2011 Page 29 of 31
Sunnyside Cogeneration Associates Unit 1

9/7/2010

Location Stack Exit - Method 7E

Average

Run Number A1 A2 A3

Test Date 6/21/2010 6/22/2010 6/22/2010

Run Start Time 12:48:00 PM 10:02:00 AM 2:47:00 PM

Run Finish Time 4:13:00 PM 2:36:00 PM 5:50:00 PM

Carbon Dioxide, % 13.7 15 14.8 14.500

Oxygen, % 5.4 4.4 4.6 4.800

Fuel Factor 1.13 1.1 1.1

Dry Volumetric Flow Rate, dry scfm 159.59 152671 149447 100,759.197

F-Factor, dscfm/MMBtu @ %O2 10284 10355 10355 10,331.333

Moisture, % 10.5 11.8 11.6 11.300

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 1000 1000 1000 1,000.000

Operating Units ppm ppm ppm

No. Readings/Avg. 60 60 60 60.000

Calibration Set 70 71 71 70.667

Calibration Pre Zero Cylinder ID 00-Zero 00-Zero 00-Zero

Calibration Pre Zero Cylinder Instrument Response -0.2 -1.8 -1.6 -1.200

Calibration Pre Zero Cylinder Bias 0 -0.33 -0.25 -0.193

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC154255-

NOX

CC154255-

NOX

CC154255-

NOX

Calibration Pre High Cylinder Instrument Response 132.7 128.3 134.5 131.833

Calibration Pre High Cylinder Bias 0.33 -0.96 1.63 0.333

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID 00-Zero 00-Zero 00-Zero

Calibration Post Zero Cylinder Instrument Response -1 -1.6 -1.3 -1.300

Calibration Post Zero Cylinder Bias -0.33 -0.25 -0.13 -0.237

Calibration Post Zero Cylinder Drift 0.33 0.08 0.12 0.177

Calibration Post High Cylinder ID CC154255-

NOX

CC154255-

NOX

CC154255-

NOX

Calibration Post High Cylinder Instrument Response 126.8 134.5 135.2 132.167

Calibration Post High Cylinder Bias -2.13 1.63 1.92 0.473

Calibration Post High Cylinder Drift 2.46 2.59 0.29 1.780

Cavg 99.2 110.4 119.2 109.600

Cavg Units ppmvd ppmvd ppmvd

Cgas 102.518 112.7738 118.5256 111.272

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

Friday, February 18, 2011 Page 30 of 31
Sunnyside Cogeneration Associates Unit 1

9/7/2010

Location Stack Exit - OTM - 27/28

Average

Run Number 1 2 3

Test Date 6/21/2010 6/23/2010 6/24/2010

Run Start Time 12:58:00 PM 9:38:00 AM 8:20:00 AM

Run Finish Time 7:49:00 PM 5:21:00 PM 4:15:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 450 450 450

Nozzle Diameter, inches 0.145 0.145 0.145 0.145

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.0045 1.0045 1.0045 1.005

Barometric Pressure, inches of Mercury 23.89 23.78 23.68 23.783

Average Orifice Meter Differential, inches H2O 0.45 0.45 0.45 0.450

Dry Gas Meter Volume Sampled, cubic feet 179.580 185.720 182.830 182.710

Average Dry Gas Meter Temperature, °F 86.96 79.96 82.00 82.973

Dry Gas Meter Volume Sampled, dscf 139.233 145.189 141.794 142.072

Total Moisture Liquid collected, g 291.9 405.6 384.2 360.567

Volume of Water Vapor, standard cubic feet 13.74 19.09 18.08 16.970

Moisture Content of Stack Gas, % 8.98 11.62 11.31 10.637

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

Dry Mole Fraction 0.9102 0.8838 0.8869 0.894

Carbon Dioxide, % 15.3 15.6 14.9 15.267

Oxygen, % 4.3 4.3 4.52 4.373

Carbon Monoxide & Nitrogen, % 80.4 80.1 80.58 80.360

Fuel Factor 1.08 1.06 1.10

Dry Molecular Weight, lb/lb-Mole 30.62 30.67 30.56 30.617

Wet Molecular weight, lb/lb-Mole 29.49 29.20 29.14 29.277

Flue Gas Static Pressure, inches of H2O -0.8 -0.8 -0.8 -0.800

Absolute Flue Gas Pressure, inches of Mercury 23.83 23.72 23.62 23.723

Average Stack Gas Temperature, °F 314.58 315.08 316.17 315.277

Average Velocity Head, inches of H2O 1.5713974384

6879

1.463963967

34344

1.538217059

70941

1.525

Average Stack Gas Velocity, feet/second 94.51 91.91 94.58 93.667

Stack Cross-Sectional Area, square feet 56.745 56.745 56.745 56.745

Dry Volumetric Flow Rate, dry scfm 159,009.7 149,360.6 153,372.7 153,914.333

Actual Wet Volumetric Flue Gas Flow Rate, acfm 321,778.2 312,926.0 322,016.5 318,906.900

Percent Isokinetic of Sampling Rate, % 96.3 106.9 101.7 101.633

Percent Excess Air, % 25.4 25.5 27.0 25.967

F-Factor, dscfm/MMBtu @ %O2 10284 10233 10308 10,275.000

Round Duct Diameter, inches 102 102 102

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

Friday, February 18, 2011 Page 31 of 31