Name: Lorna Lynum

Title: Senior Environmental Specialist

Company: Ravenswood Generating Station

Sign Date: 10/15/2010

Name: Lenny Katerynczuk

Title: Project Manager

Company: AirNova, Inc.

Sign Date: 10/15/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Ravenswood Unit 20 Utility MACT ICR

Final Test Report 

for

/ /

Based on information and belief formed 

after reasonable inquiry, I certify that the 

statements and information in this test 

report are true, accurate, and complete.

I have reviewed all testing details and 

results in this test report and hereby 

certify that the test report is authentic 

and accurate.

Monday, February 28, 2011 Page 1 of 32
Ravenswood Unit 20 Utility MACT ICR

10/15/2010

Facility Information:

Ravenswood Generating Station

38-54 Vernon Blvd

Queens NY 11101

Contact: Kenneth Yager

Phone: (718) 706-2702

Fax:

Email: kenneth_yager@transcanada.com

Testing Company:

Air Nova, Inc.

5845 Clayton Avenue

Pennsauken NJ 08109

Contact:Lenny D. Katerynczuk

Phone: 856-486-1500

Fax: 856-486-9896

Email: lenny@airnova.com

Air Permit Number:

2-6304-00024/00029

Permitted Source ID/Name:

Ravenswood Generating Station

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

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

 process flow diagram:

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 3608100002 FRS #: 110033146165

SCC / Description 10100404 External Combustion Boilers - Electric Generation - Residual Oil - Grade 6 Oil: 

Tangential Firing 

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 162 0 0 162 324 1296 2 6

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

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

Regulation Description Compound Limit Unit

Clean Air Act Section 112 0

Monday, February 28, 2011 Page 2 of 32
Ravenswood Unit 20 Utility MACT ICR

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Stack Exit 1,2,3,7,8,9-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 3 480 0

Stack Exit Other PeCDD Method 23 3 480 0

Stack Exit Other HxCDD Method 23 3 480 0

Stack Exit Other HpCDD Method 23 3 480 0

Stack Exit Other TCDF Method 23 3 480 0

Stack Exit Other PeCDF Method 23 3 480 0

Stack Exit Other HxCDF Method 23 3 480 0

Stack Exit Other HpCDF Method 23 3 480 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

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

HxCB (PCBs156/157)

Stack Exit 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

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

(PCB189)

Stack Exit Method 23 3 480 0

Stack Exit Total PCBs Method 23 3 480 0

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 3 120 0

Stack Exit Hydrogen Chloride Method 26A 3 180 0

Stack Exit Hydrogen Fluoride Method 26A 3 180 0

Inorganic (Aqueous) 

Condensible Part.

Stack Exit OTM - 27/28 3 362 0

Stack Exit Total PM2.5 OTM - 27/28 3 362 0

Organic Condensible 

Particulate

Stack Exit OTM - 27/28 3 362 0

Stack Exit Filterable Particulate OTM - 27/28 3 362 0

Stack Exit Beryllium Method 29 3 360 0

Stack Exit Cadmium Method 29 3 360 0

Stack Exit Antimony Method 29 3 360 0

Stack Exit Manganese Method 29 3 360 0

Stack Exit Cobalt Method 29 3 360 0

Stack Exit Chromium Method 29 3 360 0

Monday, February 28, 2011 Page 3 of 32
Ravenswood Unit 20 Utility MACT ICR

10/15/2010

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.

Stack Exit Lead Method 29 3 360 0

Stack Exit Selenium Method 29 3 360 0

Stack Exit Nickel Method 29 3 360 0

Stack Exit Arsenic Method 29 3 360 0

Stack Exit Filterable Particulate Method 5 3 360 0

Stack Exit Sulfur Dioxide Method 6C 3 180 0

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

Monday, February 28, 2011 Page 4 of 32
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Sampling / Stack Data Results Summary

Location Stack Exit - Method 0011

Average

Run Number 1 2 3

Test Date 8/9/2010 8/9/2010 8/9/2010

Run Start Time 9:05:00 AM 12:00:00 

PM

2:45:00 PM

Run Finish Time 11:28:00 AM 2:17:00 PM 5:05:00 PM

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 81.430 82.284 80.317 81.344

Moisture Content of Stack Gas, % 13.44 13.27 13.36 13.357

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

Carbon Dioxide, % 8.74 8.68 8.76 8.727

Oxygen, % 7.21 7.2 7.15 7.187

Average Stack Gas Temperature, °F 269.50 273.50 273.58 272.193

Dry Volumetric Flow Rate, dry scfm 621,771.6 631,454.1 626,062.2 626,429.300

Actual Wet Volumetric Flue Gas Flow Rate, acfm 979,671.9 999,081.6 993,327.4 990,693.633

Percent Isokinetic of Sampling Rate, % 99.1 98.6 97.1 98.267

F-Factor, dscfm/MMBtu @ %O2 8830 8830 8830 8,830.000

Fw 10538 10538 10538 10,538.000

Fc 1135 1040 1040 1,071.667

Location Stack Exit - Method 10

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Monday, February 28, 2011 Page 5 of 32
Ravenswood Unit 20 Utility MACT ICR

10/15/2010

Location Stack Exit - Method 10 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack Exit - Method 23

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Monday, February 28, 2011 Page 6 of 32
Ravenswood Unit 20 Utility MACT ICR

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Location Stack Exit - Method 25A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack Exit - Method 26A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Monday, February 28, 2011 Page 7 of 32
Ravenswood Unit 20 Utility MACT ICR

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Location Stack Exit - Method 29

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Location Stack Exit - Method 5

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Monday, February 28, 2011 Page 8 of 32
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Location Stack Exit - Method 6C

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack Exit - Method 7E

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Monday, February 28, 2011 Page 9 of 32
Ravenswood Unit 20 Utility MACT ICR

10/15/2010

Location Stack Exit - OTM - 27/28

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Monday, February 28, 2011 Page 10 of 32
Ravenswood Unit 20 Utility MACT ICR

10/15/2010

Emissions Summary

Location: Stack Exit - Method 0011

Compound: Formaldehyde

Average

RunNumber 1 2 3

Mass_mg 0.00615 0.00625 0.0133 0.009

lb/mmBtuO2 2.24E-06 2.26E-06 4.90E-06 0.000

ppm 2.14E-03 2.15E-03 4.68E-03 0.003

ppm@7%O2 2.17E-03 2.18E-03 4.73E-03 0.003

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 9.53E-03 1.03E-02 1.51E-02 0.012

ppm 9.72E+00 1.05E+01 1.55E+01 11.907

ppm@7%O2 9.87E+00 1.07E+01 1.57E+01 12.090

Location: Stack Exit - Method 10 3

Compound: Carbon Monoxide

Average

Run 4 5 6

lb/mmBtuO2 1.17E-03 5.05E-03 3.43E-03 0.003

ppm 1.16E+00 5.07E+00 3.51E+00 3.247

ppm@7%O2 1.21E+00 5.23E+00 3.55E+00 3.330

Location: Stack Exit - Method 23

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000167 0.00000000313 0.0000000048 0.000

lb/mmBtuO2 1.49E-13 2.84E-13 4.75E-13 0.000

ng/dscm 1.72E-04 3.32E-04 5.66E-04 0.000

ng/dscm@7%O2 1.80E-04 3.43E-04 5.73E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000057 0.0000000054 0.0000000185 0.000

lb/mmBtuO2 5.07E-13 4.90E-13 1.83E-12 0.000

ng/dscm 5.85E-04 5.73E-04 2.18E-03 0.001

ng/dscm@7%O2 6.12E-04 5.91E-04 2.21E-03 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000057 0.0000000054 0.0000000185 0.000

lb/mmBtuO2 5.07E-13 4.90E-13 1.83E-12 0.000

ng/dscm 5.85E-04 5.73E-04 2.18E-03 0.001

ng/dscm@7%O2 6.12E-04 5.91E-04 2.21E-03 0.001

Monday, February 28, 2011 Page 11 of 32
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Compound: 1,2,3,4,7,8-HxCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000142 0.00000000142 0.00000000158 0.000

lb/mmBtuO2 1.26E-13 1.29E-13 1.56E-13 0.000

ng/dscm 1.46E-04 1.51E-04 1.86E-04 0.000

ng/dscm@7%O2 1.53E-04 1.56E-04 1.88E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000421 0.00000000274 0.00000000802 0.000

lb/mmBtuO2 3.75E-13 2.49E-13 7.93E-13 0.000

ng/dscm 4.32E-04 2.91E-04 9.45E-04 0.001

ng/dscm@7%O2 4.52E-04 3.00E-04 9.57E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000142 0.00000000142 0.00000000158 0.000

lb/mmBtuO2 1.26E-13 1.29E-13 1.56E-13 0.000

ng/dscm 1.46E-04 1.51E-04 1.86E-04 0.000

ng/dscm@7%O2 1.53E-04 1.56E-04 1.88E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000421 0.00000000274 0.00000000802 0.000

lb/mmBtuO2 3.75E-13 2.49E-13 7.93E-13 0.000

ng/dscm 4.32E-04 2.91E-04 9.45E-04 0.001

ng/dscm@7%O2 4.52E-04 3.00E-04 9.57E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000142 0.00000000142 0.00000000158 0.000

lb/mmBtuO2 1.26E-13 1.29E-13 1.56E-13 0.000

ng/dscm 1.46E-04 1.51E-04 1.86E-04 0.000

ng/dscm@7%O2 1.53E-04 1.56E-04 1.88E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000421 0.00000000274 0.00000000802 0.000

lb/mmBtuO2 3.75E-13 2.49E-13 7.93E-13 0.000

ng/dscm 4.32E-04 2.91E-04 9.45E-04 0.001

ng/dscm@7%O2 4.52E-04 3.00E-04 9.57E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000131 0.00000000154 0.00000000138 0.000

lb/mmBtuO2 1.17E-13 1.40E-13 1.36E-13 0.000

Monday, February 28, 2011 Page 12 of 32
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ng/dscm 1.35E-04 1.64E-04 1.63E-04 0.000

ng/dscm@7%O2 1.41E-04 1.69E-04 1.65E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000608 0.0000000036 0.0000000064 0.000

lb/mmBtuO2 5.41E-13 3.27E-13 6.33E-13 0.000

ng/dscm 6.25E-04 3.82E-04 7.54E-04 0.001

ng/dscm@7%O2 6.54E-04 3.94E-04 7.63E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.000000031 0.0000000316 0.0000000337 0.000

lb/mmBtuO2 2.76E-12 2.87E-12 3.33E-12 0.000

ng/dscm 3.18E-03 3.36E-03 3.97E-03 0.004

ng/dscm@7%O2 3.33E-03 3.47E-03 4.02E-03 0.004

Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC

Average

RunNumber 1 2 3

Mass_mg 0.000000858 0.0000002871 0.0000003428 0.000

lb/mmBtuO2 7.64E-11 2.61E-11 3.39E-11 0.000

ng/dscm 8.81E-02 3.05E-02 4.04E-02 0.053

ng/dscm@7%O2 9.21E-02 3.15E-02 4.09E-02 0.055

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

Average

RunNumber 1 2 3

Mass_mg 0.00000108 0.000000681 0.000000851 0.000

lb/mmBtuO2 9.62E-11 6.18E-11 8.42E-11 0.000

ng/dscm 1.11E-01 7.23E-02 1.00E-01 0.094

ng/dscm@7%O2 1.16E-01 7.46E-02 1.01E-01 0.097

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

Average

RunNumber 1 2 3

Mass_mg 0.000000178 0.000000131 0.000000148 0.000

lb/mmBtuO2 1.58E-11 1.19E-11 1.46E-11 0.000

ng/dscm 1.83E-02 1.39E-02 1.74E-02 0.017

ng/dscm@7%O2 1.91E-02 1.43E-02 1.76E-02 0.017

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000874 0.0000000481 0.0000000597 0.000

lb/mmBtuO2 7.78E-12 4.37E-12 5.90E-12 0.000

ng/dscm 8.98E-03 5.11E-03 7.03E-03 0.007

ng/dscm@7%O2 9.39E-03 5.27E-03 7.12E-03 0.007

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

Average

RunNumber 1 2 3

Monday, February 28, 2011 Page 13 of 32
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Mass_mg 0.0000037 0.00000196 0.00000252 0.000

lb/mmBtuO2 3.29E-10 1.78E-10 2.49E-10 0.000

ng/dscm 3.80E-01 2.08E-01 2.97E-01 0.295

ng/dscm@7%O2 3.97E-01 2.15E-01 3.01E-01 0.304

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000605 0.0000000407 0.0000000559 0.000

lb/mmBtuO2 5.39E-12 3.70E-12 5.53E-12 0.000

ng/dscm 6.21E-03 4.32E-03 6.59E-03 0.006

ng/dscm@7%O2 6.50E-03 4.46E-03 6.67E-03 0.006

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000421 0.00000000274 0.00000000802 0.000

lb/mmBtuO2 3.75E-13 2.49E-13 7.93E-13 0.000

ng/dscm 4.32E-04 2.91E-04 9.45E-04 0.001

ng/dscm@7%O2 4.52E-04 3.00E-04 9.57E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000427 0.000000003 0.00000000595 0.000

lb/mmBtuO2 3.80E-13 2.72E-13 5.88E-13 0.000

ng/dscm 4.39E-04 3.19E-04 7.01E-04 0.000

ng/dscm@7%O2 4.59E-04 3.29E-04 7.10E-04 0.000

Compound: 2,3,7,8-TCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000108 0.00000000095 0.00000000072 0.000

lb/mmBtuO2 9.62E-14 8.63E-14 7.12E-14 0.000

ng/dscm 1.11E-04 1.01E-04 8.48E-05 0.000

ng/dscm@7%O2 1.16E-04 1.04E-04 8.58E-05 0.000

Compound: 2,3,7,8-TCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000000373 0.00000000272 0.00000000333 0.000

lb/mmBtuO2 3.32E-13 2.47E-13 3.29E-13 0.000

ng/dscm 3.83E-04 2.89E-04 3.92E-04 0.000

ng/dscm@7%O2 4.01E-04 2.98E-04 3.97E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000518 0.00000000789 0.00000000622 0.000

lb/mmBtuO2 4.61E-13 7.17E-13 6.15E-13 0.000

ng/dscm 5.32E-04 8.38E-04 7.33E-04 0.001

ng/dscm@7%O2 5.56E-04 8.65E-04 7.42E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000231 0.0000000179 0.0000000179 0.000

lb/mmBtuO2 2.06E-12 1.63E-12 1.77E-12 0.000

ng/dscm 2.37E-03 1.90E-03 2.11E-03 0.002

ng/dscm@7%O2 2.48E-03 1.96E-03 2.14E-03 0.002

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

Average

RunNumber 1 2 3

Mass_mg 0.000000246 0.000000144 0.000000151 0.000

lb/mmBtuO2 2.19E-11 1.31E-11 1.49E-11 0.000

ng/dscm 2.53E-02 1.53E-02 1.78E-02 0.019

ng/dscm@7%O2 2.65E-02 1.58E-02 1.80E-02 0.020

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000192 0.0000000106 0.0000000115 0.000

lb/mmBtuO2 1.71E-12 9.63E-13 1.14E-12 0.000

ng/dscm 1.97E-03 1.13E-03 1.36E-03 0.001

ng/dscm@7%O2 2.06E-03 1.17E-03 1.38E-03 0.002

Compound: OCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000844 0.0000000215 0.0000000175 0.000

lb/mmBtuO2 7.51E-13 1.95E-12 1.73E-12 0.000

ng/dscm 8.67E-04 2.28E-03 2.06E-03 0.002

ng/dscm@7%O2 9.07E-04 2.35E-03 2.09E-03 0.002

Compound: OCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000000482 0.00000000453 0.00000000776 0.000

lb/mmBtuO2 4.29E-13 4.11E-13 7.67E-13 0.000

ng/dscm 4.95E-04 4.81E-04 9.14E-04 0.001

ng/dscm@7%O2 5.18E-04 4.96E-04 9.25E-04 0.001

Compound: Other HpCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000294 0.00000000807 0.00000000648 0.000

lb/mmBtuO2 2.62E-13 7.33E-13 6.41E-13 0.000

ng/dscm 3.02E-04 8.57E-04 7.64E-04 0.001

ng/dscm@7%O2 3.16E-04 8.84E-04 7.73E-04 0.001

Compound: Other HpCDF

Average

RunNumber 1 2 3

Mass_mg 0 0 0.00000000621 0.000

lb/mmBtuO2 0.00E+00 0.00E+00 6.14E-13 0.000

Monday, February 28, 2011 Page 15 of 32
Ravenswood Unit 20 Utility MACT ICR

10/15/2010

ng/dscm 0.00E+00 0.00E+00 7.32E-04 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 7.41E-04 0.000

Compound: Other HxCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000282 0.00000000537 0.00000000524 0.000

lb/mmBtuO2 2.51E-13 4.88E-13 5.18E-13 0.000

ng/dscm 2.90E-04 5.70E-04 6.17E-04 0.000

ng/dscm@7%O2 3.03E-04 5.88E-04 6.25E-04 0.001

Compound: Other HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.000000022 0.000000013 0.0000000294 0.000

lb/mmBtuO2 1.96E-12 1.18E-12 2.91E-12 0.000

ng/dscm 2.26E-03 1.38E-03 3.46E-03 0.002

ng/dscm@7%O2 2.36E-03 1.42E-03 3.50E-03 0.002

Compound: Other PeCDD

Average

RunNumber 1 2 3

Mass_mg 0 0.00000000284 0.00000000236 0.000

lb/mmBtuO2 0.00E+00 2.58E-13 2.33E-13 0.000

ng/dscm 0.00E+00 3.02E-04 2.78E-04 0.000

ng/dscm@7%O2 0.00E+00 3.12E-04 2.81E-04 0.000

Compound: Other PeCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000429 0.0000000213 0.000000057 0.000

lb/mmBtuO2 3.82E-12 1.93E-12 5.64E-12 0.000

ng/dscm 4.41E-03 2.26E-03 6.72E-03 0.004

ng/dscm@7%O2 4.61E-03 2.33E-03 6.80E-03 0.005

Compound: Other TCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000331 0.00000000531 0.00000000434 0.000

lb/mmBtuO2 2.95E-13 4.82E-13 4.29E-13 0.000

ng/dscm 3.40E-04 5.64E-04 5.11E-04 0.000

ng/dscm@7%O2 3.56E-04 5.82E-04 5.17E-04 0.000

Compound: Other TCDF

Average

RunNumber 1 2 3

Mass_mg 0.000000045 0.0000000239 0.0000000588 0.000

lb/mmBtuO2 4.01E-12 2.17E-12 5.81E-12 0.000

ng/dscm 4.62E-03 2.54E-03 6.93E-03 0.005

ng/dscm@7%O2 4.83E-03 2.62E-03 7.02E-03 0.005

Compound: Total Dioxins

Average

RunNumber 1 2 3

Monday, February 28, 2011 Page 16 of 32
Ravenswood Unit 20 Utility MACT ICR

10/15/2010

Mass_mg 0.00000002583 0.00000005297 0.00000004756 0.000

lb/mmBtuO2 2.30E-12 4.81E-12 4.70E-12 0.000

ng/dscm 2.65E-03 5.63E-03 5.60E-03 0.005

ng/dscm@7%O2 2.77E-03 5.81E-03 5.67E-03 0.005

Compound: Total Furans

Average

RunNumber 1 2 3

Mass_mg 0.00000015704 0.00000009381 0.00000024393 0.000

lb/mmBtuO2 1.40E-11 8.52E-12 2.41E-11 0.000

ng/dscm 1.61E-02 9.96E-03 2.87E-02 0.018

ng/dscm@7%O2 1.68E-02 1.03E-02 2.91E-02 0.019

Compound: Total PCBs

Average

RunNumber 1 2 3

Mass_mg 0.00000628838 0.00000335989 0.00000419772 0.000

lb/mmBtuO2 5.60E-10 3.05E-10 4.15E-10 0.000

ng/dscm 6.46E-01 3.57E-01 4.95E-01 0.499

ng/dscm@7%O2 6.76E-01 3.68E-01 5.01E-01 0.515

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 1.78E-04 1.78E-04 1.77E-04 0.000

ppm 1.15E-01 1.15E-01 1.15E-01 0.115

ppm@7%O2 1.17E-01 1.17E-01 1.16E-01 0.117

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 0.79 1.05 0.94 0.927

lb/mmBtuO2 2.04E-04 2.72E-04 2.37E-04 0.000

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.71 0.64 0.65 0.667

lb/mmBtuO2 1.83E-04 1.66E-04 1.64E-04 0.000

Location: Stack Exit - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.312748 0.31118 0.267509 0.297

lb/mmBtuO2 4.02E-05 3.93E-05 3.25E-05 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Monday, February 28, 2011 Page 17 of 32
Ravenswood Unit 20 Utility MACT ICR

10/15/2010

Mass_mg 0.004037 0.003504 0.002585 0.003

lb/mmBtuO2 5.18E-07 4.43E-07 3.14E-07 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.000839 0.000716 0.000587 0.001

lb/mmBtuO2 1.08E-07 9.05E-08 7.14E-08 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.001189 0.000569 0.000473 0.001

lb/mmBtuO2 1.53E-07 7.19E-08 5.75E-08 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.04053 0.01113 0.006284 0.019

lb/mmBtuO2 5.20E-06 1.41E-06 7.64E-07 0.000

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.043108 0.04 0.0325 0.039

lb/mmBtuO2 5.54E-06 5.06E-06 3.95E-06 0.000

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.00888 0.00912 0.005847 0.008

lb/mmBtuO2 1.14E-06 1.15E-06 7.11E-07 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.10252 0.08327 0.07563 0.087

lb/mmBtuO2 1.32E-05 1.05E-05 9.20E-06 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.66096 0.60688 0.54351 0.604

lb/mmBtuO2 8.49E-05 7.67E-05 6.61E-05 0.000

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.003612 0.004014 0.002002 0.003

lb/mmBtuO2 4.64E-07 5.07E-07 2.44E-07 0.000

Location: Stack Exit - Method 5

Monday, February 28, 2011 Page 18 of 32
Ravenswood Unit 20 Utility MACT ICR

10/15/2010

Process Run Data

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 14.8 15.2 14.8 14.933

lb/mmBtuO2 1.90E-03 1.92E-03 1.80E-03 0.002

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

lb/mmBtuO2 4.31E-02 5.64E-02 4.09E-02 0.047

ppm 1.85E+01 2.41E+01 1.80E+01 20.200

ppm@7%O2 1.95E+01 2.56E+01 1.85E+01 21.200

Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

lb/mmBtuO2 2.14E-01 1.93E-01 1.58E-01 0.188

ppm 1.28E+02 1.15E+02 9.66E+01 113.200

ppm@7%O2 1.35E+02 1.22E+02 9.95E+01 118.833

Location: Stack Exit - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 9.7 10.3 8.9 9.633

lb/mmBtuO2 2.01E-03 2.11E-03 1.80E-03 0.002

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 11.3 20.9 6.2 12.800

lb/mmBtuO2 2.34E-03 4.28E-03 1.26E-03 0.003

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 4.1 7.6 1 4.233

lb/mmBtuO2 8.49E-04 1.56E-03 2.03E-04 0.001

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 25.1 38.8 16.1 26.667

lb/mmBtuO2 5.20E-03 7.95E-03 3.26E-03 0.005

Monday, February 28, 2011 Page 19 of 32
Ravenswood Unit 20 Utility MACT ICR

10/15/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Residual Oil (No. 6) Burned 4754.9 Gallons/hr 0

10 Residual Oil (No. 6) Burned 4771 Gallons/hr 0

11 Residual Oil (No. 6) Burned 4738.5 Gallons/hr 0

12 Residual Oil (No. 6) Burned 5384.3 Gallons/hr 0

2 Residual Oil (No. 6) Burned 5237 Gallons/hr 0

3 Residual Oil (No. 6) Burned 4739.2 Gallons/hr 0

4 Residual Oil (No. 6) Burned 4757.3 Gallons/hr 0

5 Residual Oil (No. 6) Burned 5347.3 Gallons/hr 0

6 Residual Oil (No. 6) Burned 4688.9 Gallons/hr 0

7 Residual Oil (No. 6) Burned 5439.8 Gallons/hr 0

8 Residual Oil (No. 6) Burned 5339.7 Gallons/hr 0

9 Residual Oil (No. 6) Burned 5187.4 Gallons/hr 0

1 Natural Gas Burned 2387.8 Decatherms 0

10 Natural Gas Burned 2364.6 Decatherms 0

11 Natural Gas Burned 2362 Decatherms 0

12 Natural Gas Burned 2303 Decatherms 0

2 Natural Gas Burned 2299 Decatherms 0

3 Natural Gas Burned 2353.1 Decatherms 0

4 Natural Gas Burned 2371.4 Decatherms 0

5 Natural Gas Burned 2301.4 Decatherms 0

6 Natural Gas Burned 2358 Decatherms 0

7 Natural Gas Burned 2367.1 Decatherms 0

8 Natural Gas Burned 2382.3 Decatherms 0

9 Natural Gas Burned 2391.5 Decatherms 0

1 Steam Generation Rate 2282 1,000 lb/hr 0

10 Steam Generation Rate 2277.8 1,000 lb/hr 0

11 Steam Generation Rate 2274.7 1,000 lb/hr 0

12 Steam Generation Rate 2277.1 1,000 lb/hr 0

2 Steam Generation Rate 2276.7 1,000 lb/hr 0

3 Steam Generation Rate 2268.9 1,000 lb/hr 0

4 Steam Generation Rate 2278.9 1,000 lb/hr 0

5 Steam Generation Rate 2277.1 1,000 lb/hr 0

6 Steam Generation Rate 2261.5 1,000 lb/hr 0

Monday, February 28, 2011 Page 20 of 32
Ravenswood Unit 20 Utility MACT ICR

10/15/2010

APCD Run Data

Process Lab Run Data

7 Steam Generation Rate 2381.9 1,000 lb/hr 0

8 Steam Generation Rate 2381.2 1,000 lb/hr 0

9 Steam Generation Rate 2379.4 1,000 lb/hr 0

1 Net Electrical Output 321.41 MWe 0

10 Net Electrical Output 320.84 MWe 0

11 Net Electrical Output 320.39 MWe 0

12 Net Electrical Output 320.72 MWe 0

2 Net Electrical Output 320.66 MWe 0

3 Net Electrical Output 319.56 MWe 0

4 Net Electrical Output 320.98 MWe 0

5 Net Electrical Output 320.71 MWe 0

6 Net Electrical Output 318.51 MWe 0

7 Net Electrical Output 335.5 MWe 0

8 Net Electrical Output 335.39 MWe 0

9 Net Electrical Output 335.13 MWe 0

1 Gross Electrical Output 311.02 MWh 0

10 Gross Electrical Output 310.43 MWh 0

11 Gross Electrical Output 310.27 MWh 0

12 Gross Electrical Output 310.62 MWh 0

2 Gross Electrical Output 310.43 MWh 0

3 Gross Electrical Output 309.39 MWh 0

4 Gross Electrical Output 310.62 MWh 0

5 Gross Electrical Output 310.57 MWh 0

6 Gross Electrical Output 308.3 MWh 0

7 Gross Electrical Output 325.14 MWh 0

8 Gross Electrical Output 324.89 MWh 0

9 Gross Electrical Output 324.81 MWh 0

Monday, February 28, 2011 Page 21 of 32
Ravenswood Unit 20 Utility MACT ICR

10/15/2010

Sampling / Stack Data Results Detail

Location Stack Exit - Method 0011

Average

Run Number 1 2 3

Test Date 8/9/2010 8/9/2010 8/9/2010

Run Start Time 9:05:00 AM 12:00:00 PM 2:45:00 PM

Run Finish Time 11:28:00 AM 2:17:00 PM 5:05:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 120 120 120

Nozzle Diameter, inches 0.17 0.17 0.17 0.170

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 30.03 30.01 29.96 30.000

Average Orifice Meter Differential, inches H2O 1.57 1.62 1.59 1.593

Dry Gas Meter Volume Sampled, cubic feet 84.703 86.837 84.538 85.359

Average Dry Gas Meter Temperature, °F 87.83 95.50 93.08 92.137

Dry Gas Meter Volume Sampled, dscf 81.430 82.284 80.317 81.344

Total Moisture Liquid collected, g 268.5 267.5 263.2 266.400

Volume of Water Vapor, standard cubic feet 12.64 12.59 12.39 12.540

Moisture Content of Stack Gas, % 13.44 13.27 13.36 13.357

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

Dry Mole Fraction 0.8656 0.8673 0.8664 0.866

Carbon Dioxide, % 8.74 8.68 8.76 8.727

Oxygen, % 7.21 7.2 7.15 7.187

Carbon Monoxide & Nitrogen, % 84.05 84.12 84.09 84.087

Fuel Factor 1.57 1.58 1.57

Dry Molecular Weight, lb/lb-Mole 29.69 29.68 29.69 29.687

Wet Molecular weight, lb/lb-Mole 28.12 28.13 28.13 28.127

Flue Gas Static Pressure, inches of H2O 3.8 3.8 3.8 3.800

Absolute Flue Gas Pressure, inches of Mercury 30.31 30.29 30.24 30.280

Average Stack Gas Temperature, °F 269.50 273.50 273.58 272.193

Average Velocity Head, inches of H2O 2.9479596477

2622

3.048560222

46397

3.007853344

17391

3.001

Average Stack Gas Velocity, feet/second 114.07 116.33 115.66 115.353

Stack Cross-Sectional Area, square feet 143.139 143.139 143.139 143.139

Dry Volumetric Flow Rate, dry scfm 621,771.6 631,454.1 626,062.2 626,429.300

Actual Wet Volumetric Flue Gas Flow Rate, acfm 979,671.9 999,081.6 993,327.4 990,693.633

Percent Isokinetic of Sampling Rate, % 99.1 98.6 97.1 98.267

Percent Excess Air, % 48.1 48.0 47.5 47.867

F-Factor, dscfm/MMBtu @ %O2 8830 8830 8830 8,830.000

Round Duct Diameter, inches 162 162 162

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10538 10538 10538 10,538.000

Fc 1135 1040 1040 1,071.667

Monday, February 28, 2011 Page 22 of 32
Ravenswood Unit 20 Utility MACT ICR

10/15/2010

Location Stack Exit - Method 10

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Monday, February 28, 2011 Page 23 of 32
Ravenswood Unit 20 Utility MACT ICR

10/15/2010

Location Stack Exit - Method 10 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Monday, February 28, 2011 Page 24 of 32
Ravenswood Unit 20 Utility MACT ICR

10/15/2010

Location Stack Exit - Method 23

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Monday, February 28, 2011 Page 25 of 32
Ravenswood Unit 20 Utility MACT ICR

10/15/2010

Location Stack Exit - Method 25A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Monday, February 28, 2011 Page 26 of 32
Ravenswood Unit 20 Utility MACT ICR

10/15/2010

Location Stack Exit - Method 26A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Monday, February 28, 2011 Page 27 of 32
Ravenswood Unit 20 Utility MACT ICR

10/15/2010

Location Stack Exit - Method 29

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Monday, February 28, 2011 Page 28 of 32
Ravenswood Unit 20 Utility MACT ICR

10/15/2010

Location Stack Exit - Method 5

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Monday, February 28, 2011 Page 29 of 32
Ravenswood Unit 20 Utility MACT ICR

10/15/2010

Location Stack Exit - Method 6C

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Monday, February 28, 2011 Page 30 of 32
Ravenswood Unit 20 Utility MACT ICR

10/15/2010

Location Stack Exit - Method 7E

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Monday, February 28, 2011 Page 31 of 32
Ravenswood Unit 20 Utility MACT ICR

10/15/2010

Location Stack Exit - OTM - 27/28

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Monday, February 28, 2011 Page 32 of 32