Name:

Title:

Company:

Sign Date:

Name: Brian Durkop

Title: Vice President

Company: EMSI

Sign Date: 9/4/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Dynegy Danskammer 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 11, 2011 Page 1 of 32
Dynegy Danskammer Unit 1

Facility Information:

Dynegy Danskammer Generating Station

994 River Road

Newburgh NY 12550

Contact: Andrew Matura

Phone: 845-563-4923

Fax: 845-563-4992

Email: andrew.d.matura@dynegy.com

Testing Company:

Eagle Mountain Scientific, Inc.

8905 Autumn Oaks Drive

Suite 2

Rockford MN 55373

Contact:Brian Durkop

Phone: 763-477-4462

Fax: 763-477-5991

Email: bdurkop@eagle-msi.com

Air Permit Number:

3-3346-00011/00002

Permitted Source ID/Name:

1 Unit 1

Permitted Maximum Process Rate:

NA

Max. Normal Operation Process Rate:

74 MW

Target Process Test Rate

40 MW

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

 process flow diagram:

Dankammer 1 is an oil fired boiler with a maximum rated capacity of 74 MW. The unit is equipped with electrostatic 

precipitators.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 3607100002 FRS #: 110041167108

SCC / Description 10100401 External Combustion Boilers - Electric Generation - Residual Oil - Grade 6 Oil: 

Normal 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 144 0 0 0 528 1020 4 24

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Exit Carbon Monoxide Method 10 3 180 0

Stack Exit Formaldehyde Method 0011 3 120 0

Stack Exit 2,3,7,8-TCDD Method 23 3 480 0

Stack Exit 1,2,3,7,8-PeCDD Method 23 3 480 0

Stack Exit 1,2,3,4,7,8-HxCDD Method 23 3 480 0

Stack Exit 1,2,3,6,7,8-HxCDD Method 23 3 480 0

Stack Exit 1,2,3,7,8,9-HxCDD Method 23 3 480 0

Friday, February 11, 2011 Page 2 of 32
Dynegy Danskammer Unit 1

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

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 3 120 0

Stack Exit Hydrogen Fluoride Method 26 3 90 0

Stack Exit Hydrogen Chloride Method 26 3 90 0

Stack Exit Total Particulate OTM - 27/28 3 360 0

Stack Exit Total PM2.5 OTM - 27/28 3 360 0

Organic Condensible 

Particulate

Stack Exit OTM - 27/28 3 360 0

Inorganic (Aqueous) 

Condensible Part.

Stack Exit OTM - 27/28 3 360 0

Stack Exit Filterable PM2.5 OTM - 27/28 3 360 0

Stack Exit Filterable Particulate OTM - 27/28 3 360 0

Stack Exit Filterable Particulate 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

Friday, February 11, 2011 Page 3 of 32
Dynegy Danskammer Unit 1

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.

None

Stack Exit Lead Method 29 3 240 0

Stack Exit Magnesium Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Selenium Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Sulfur Dioxide Method 6C 3 180 0

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

Friday, February 11, 2011 Page 4 of 32
Dynegy Danskammer Unit 1

Sampling / Stack Data Results Summary

Location Stack Exit - Method 0011

Average

Run Number 1 2

Test Date 7/20/2010 7/20/2010

Run Start Time 12:00:00 AM 12:00:00 

AM

Run Finish Time 12:14:00 PM 12:59:00 

PM

Net Run Time, minutes 120 120

Dry Gas Meter Volume Sampled, dscf 74.509 76.652 75.581

Moisture Content of Stack Gas, % 10.32 10.21 10.265

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.000

Carbon Dioxide, % 11.6 11.5 11.550

Oxygen, % 6.1 6.2 6.150

Average Stack Gas Temperature, °F 297.48 297.22 297.350

Dry Volumetric Flow Rate, dry scfm 106,564.6 109,396.1 107,980.350

Actual Wet Volumetric Flue Gas Flow Rate, acfm 171,274.1 175,549.2 173,411.650

Percent Isokinetic of Sampling Rate, % 100.9 101.1 101.000

F-Factor, dscfm/MMBtu @ %O2 9488 9488 9,488.000

Fw 0 0 0.000

Fc 0 0 0.000

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

Friday, February 11, 2011 Page 5 of 32
Dynegy Danskammer Unit 1

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

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

Friday, February 11, 2011 Page 6 of 32
Dynegy Danskammer Unit 1

Location Stack Exit - Method 26

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 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

Friday, February 11, 2011 Page 7 of 32
Dynegy Danskammer Unit 1

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

Friday, February 11, 2011 Page 8 of 32
Dynegy Danskammer Unit 1

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

Friday, February 11, 2011 Page 9 of 32
Dynegy Danskammer Unit 1

Emissions Summary

Location: Stack Exit - Method 0011

Compound: Formaldehyde

Average

RunNumber 1 2

Mass_mg 0.052 0.03 0.041

lb/mmBtuO2 2.06E-05 1.16E-05 0.000

ppm 1.97E-02 1.11E-02 0.015

ppm@7%O2 1.85E-02 1.05E-02 0.015

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2

lb/mmBtuO2 9.15E-03 2.12E-03 0.006

ppm 9.40E+00 2.16E+00 5.780

ppm@7%O2 8.83E+00 2.04E+00 5.435

Location: Stack Exit - Method 23

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

Average

RunNumber 1 2

Mass_mg 0.000000113 0.000000078 0.000

lb/mmBtuO2 1.20E-11 9.90E-12 0.000

ng/dscm 1.35E-02 1.18E-02 0.013

ng/dscm@7%O2 1.35E-02 1.11E-02 0.012

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

Average

RunNumber 1 2

Mass_mg 0.00000019 0.00000013 0.000

lb/mmBtuO2 2.02E-11 1.65E-11 0.000

ng/dscm 2.27E-02 1.97E-02 0.021

ng/dscm@7%O2 2.27E-02 1.86E-02 0.021

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

Average

RunNumber 1 2

Mass_mg 0.0000000241 0.000000013 0.000

lb/mmBtuO2 2.56E-12 1.65E-12 0.000

ng/dscm 2.88E-03 1.97E-03 0.002

ng/dscm@7%O2 2.88E-03 1.86E-03 0.002

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

Average

RunNumber 1 2

Mass_mg 0.0000000124 0.0000000095 0.000

lb/mmBtuO2 1.32E-12 1.21E-12 0.000

ng/dscm 1.48E-03 1.44E-03 0.001

ng/dscm@7%O2 1.48E-03 1.36E-03 0.001

Friday, February 11, 2011 Page 10 of 32
Dynegy Danskammer Unit 1

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

Average

RunNumber 1 2

Mass_mg 0.000000047 0.00000004 0.000

lb/mmBtuO2 4.99E-12 5.08E-12 0.000

ng/dscm 5.61E-03 6.05E-03 0.006

ng/dscm@7%O2 5.61E-03 5.70E-03 0.006

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

Average

RunNumber 1 2

Mass_mg 0.0000000171 0.000000012 0.000

lb/mmBtuO2 1.82E-12 1.52E-12 0.000

ng/dscm 2.04E-03 1.81E-03 0.002

ng/dscm@7%O2 2.04E-03 1.71E-03 0.002

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

Average

RunNumber 1 2

Mass_mg 0.000000065 0.000000049 0.000

lb/mmBtuO2 6.90E-12 6.22E-12 0.000

ng/dscm 7.76E-03 7.41E-03 0.008

ng/dscm@7%O2 7.76E-03 6.98E-03 0.007

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

Average

RunNumber 1 2

Mass_mg 0.0000000197 0.0000000118 0.000

lb/mmBtuO2 2.09E-12 1.50E-12 0.000

ng/dscm 2.35E-03 1.78E-03 0.002

ng/dscm@7%O2 2.35E-03 1.68E-03 0.002

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

Average

RunNumber 1 2

Mass_mg 0.0000000048 0.000000004 0.000

lb/mmBtuO2 5.09E-13 5.08E-13 0.000

ng/dscm 5.73E-04 6.05E-04 0.001

ng/dscm@7%O2 5.73E-04 5.70E-04 0.001

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

Average

RunNumber 1 2

Mass_mg 0.000000014 0.0000000098 0.000

lb/mmBtuO2 1.49E-12 1.24E-12 0.000

ng/dscm 1.67E-03 1.48E-03 0.002

ng/dscm@7%O2 1.67E-03 1.39E-03 0.002

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

Average

RunNumber 1 2

Mass_mg 0.000000043 0.0000000292 0.000

lb/mmBtuO2 4.56E-12 3.71E-12 0.000

Friday, February 11, 2011 Page 11 of 32
Dynegy Danskammer Unit 1

ng/dscm 5.14E-03 4.42E-03 0.005

ng/dscm@7%O2 5.14E-03 4.17E-03 0.005

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

Average

RunNumber 1 2

Mass_mg 0.000000014 0.000000012 0.000

lb/mmBtuO2 1.49E-12 1.52E-12 0.000

ng/dscm 1.67E-03 1.81E-03 0.002

ng/dscm@7%O2 1.67E-03 1.71E-03 0.002

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

Average

RunNumber 1 2

Mass_mg 0.000000038 0.000000034 0.000

lb/mmBtuO2 4.03E-12 4.31E-12 0.000

ng/dscm 4.54E-03 5.14E-03 0.005

ng/dscm@7%O2 4.54E-03 4.84E-03 0.005

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

Average

RunNumber 1 2

Mass_mg 0.0000001 0.000000078 0.000

lb/mmBtuO2 1.06E-11 9.90E-12 0.000

ng/dscm 1.19E-02 1.18E-02 0.012

ng/dscm@7%O2 1.19E-02 1.11E-02 0.012

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

Average

RunNumber 1 2

Mass_mg 0.000000015 0.000000013 0.000

lb/mmBtuO2 1.59E-12 1.65E-12 0.000

ng/dscm 1.79E-03 1.97E-03 0.002

ng/dscm@7%O2 1.79E-03 1.86E-03 0.002

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

Average

RunNumber 1 2

Mass_mg 0.000000011 0.0000000077 0.000

lb/mmBtuO2 1.17E-12 9.77E-13 0.000

ng/dscm 1.31E-03 1.16E-03 0.001

ng/dscm@7%O2 1.31E-03 1.09E-03 0.001

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

Average

RunNumber 1 2

Mass_mg 0.00000032 0.00000025 0.000

lb/mmBtuO2 3.40E-11 3.17E-11 0.000

ng/dscm 3.82E-02 3.78E-02 0.038

ng/dscm@7%O2 3.82E-02 3.56E-02 0.037

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

Average

RunNumber 1 2

Friday, February 11, 2011 Page 12 of 32
Dynegy Danskammer Unit 1

Mass_mg 0.0000000045 0.0000000049 0.000

lb/mmBtuO2 4.78E-13 6.22E-13 0.000

ng/dscm 5.38E-04 7.41E-04 0.001

ng/dscm@7%O2 5.38E-04 6.98E-04 0.001

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

Average

RunNumber 1 2

Mass_mg 0.000000056 0.000000041 0.000

lb/mmBtuO2 5.94E-12 5.20E-12 0.000

ng/dscm 6.69E-03 6.20E-03 0.006

ng/dscm@7%O2 6.69E-03 5.84E-03 0.006

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

Average

RunNumber 1 2

Mass_mg 0.00000004 0.000000031 0.000

lb/mmBtuO2 4.25E-12 3.93E-12 0.000

ng/dscm 4.78E-03 4.69E-03 0.005

ng/dscm@7%O2 4.78E-03 4.42E-03 0.005

Compound: 2,3,7,8-TCDD

Average

RunNumber 1 2

Mass_mg 0.0000000062 0.0000000043 0.000

lb/mmBtuO2 6.58E-13 5.46E-13 0.000

ng/dscm 7.41E-04 6.50E-04 0.001

ng/dscm@7%O2 7.41E-04 6.13E-04 0.001

Compound: 2,3,7,8-TCDF

Average

RunNumber 1 2

Mass_mg 0.000000059 0.000000044 0.000

lb/mmBtuO2 6.26E-12 5.58E-12 0.000

ng/dscm 7.05E-03 6.65E-03 0.007

ng/dscm@7%O2 7.05E-03 6.27E-03 0.007

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

Average

RunNumber 1 2

Mass_mg 0.000000014 0.0000000063 0.000

lb/mmBtuO2 1.49E-12 7.99E-13 0.000

ng/dscm 1.67E-03 9.53E-04 0.001

ng/dscm@7%O2 1.67E-03 8.98E-04 0.001

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

Average

RunNumber 1 2

Mass_mg 0.0000000045 0.0000000048 0.000

lb/mmBtuO2 4.78E-13 6.09E-13 0.000

ng/dscm 5.38E-04 7.26E-04 0.001

ng/dscm@7%O2 5.38E-04 6.84E-04 0.001

Friday, February 11, 2011 Page 13 of 32
Dynegy Danskammer Unit 1

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

Average

RunNumber 1 2

Mass_mg 0.000000036 0.000000018 0.000

lb/mmBtuO2 3.82E-12 2.28E-12 0.000

ng/dscm 4.30E-03 2.72E-03 0.004

ng/dscm@7%O2 4.30E-03 2.56E-03 0.003

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

Average

RunNumber 1 2

Mass_mg 0.000000011 0.0000000089 0.000

lb/mmBtuO2 1.17E-12 1.13E-12 0.000

ng/dscm 1.31E-03 1.35E-03 0.001

ng/dscm@7%O2 1.31E-03 1.27E-03 0.001

Compound: OCDD

Average

RunNumber 1 2

Mass_mg 0.000000375 0.000000222 0.000

lb/mmBtuO2 3.98E-11 2.82E-11 0.000

ng/dscm 4.48E-02 3.36E-02 0.039

ng/dscm@7%O2 4.48E-02 3.17E-02 0.038

Compound: OCDF

Average

RunNumber 1 2

Mass_mg 0.000000123 0.000000051 0.000

lb/mmBtuO2 1.31E-11 6.47E-12 0.000

ng/dscm 1.47E-02 7.71E-03 0.011

ng/dscm@7%O2 1.47E-02 7.27E-03 0.011

Compound: Other HpCDD

Average

RunNumber 1 2

Mass_mg 0.000000205 0.000000149 0.000

lb/mmBtuO2 2.18E-11 1.89E-11 0.000

ng/dscm 2.45E-02 2.25E-02 0.024

ng/dscm@7%O2 2.45E-02 2.12E-02 0.023

Compound: Other HpCDF

Average

RunNumber 1 2

Mass_mg 0.000000058 0.000000041 0.000

lb/mmBtuO2 6.16E-12 5.20E-12 0.000

ng/dscm 6.93E-03 6.20E-03 0.007

ng/dscm@7%O2 6.93E-03 5.84E-03 0.006

Compound: Other HxCDD

Average

RunNumber 1 2

Mass_mg 0.000000138 0.000000091 0.000

lb/mmBtuO2 1.46E-11 1.15E-11 0.000

Friday, February 11, 2011 Page 14 of 32
Dynegy Danskammer Unit 1

ng/dscm 1.65E-02 1.38E-02 0.015

ng/dscm@7%O2 1.65E-02 1.30E-02 0.015

Compound: Other HxCDF

Average

RunNumber 1 2

Mass_mg 0.000000308 0.000000277 0.000

lb/mmBtuO2 3.27E-11 3.51E-11 0.000

ng/dscm 3.68E-02 4.19E-02 0.039

ng/dscm@7%O2 3.68E-02 3.95E-02 0.038

Compound: Other PeCDD

Average

RunNumber 1 2

Mass_mg 0.000000092 0.000000052 0.000

lb/mmBtuO2 9.77E-12 6.60E-12 0.000

ng/dscm 1.10E-02 7.86E-03 0.009

ng/dscm@7%O2 1.10E-02 7.41E-03 0.009

Compound: Other PeCDF

Average

RunNumber 1 2

Mass_mg 0.000000422 0.000000287 0.000

lb/mmBtuO2 4.48E-11 3.64E-11 0.000

ng/dscm 5.04E-02 4.34E-02 0.047

ng/dscm@7%O2 5.04E-02 4.09E-02 0.046

Compound: Other TCDD

Average

RunNumber 1 2

Mass_mg 0.000000036 0.0000000123 0.000

lb/mmBtuO2 3.82E-12 1.56E-12 0.000

ng/dscm 4.30E-03 1.86E-03 0.003

ng/dscm@7%O2 4.30E-03 1.75E-03 0.003

Compound: Other TCDF

Average

RunNumber 1 2

Mass_mg 0.000000361 0.000000253 0.000

lb/mmBtuO2 3.83E-11 3.21E-11 0.000

ng/dscm 4.31E-02 3.83E-02 0.041

ng/dscm@7%O2 4.31E-02 3.61E-02 0.040

Compound: Total Dioxins

Average

RunNumber 1 2

Mass_mg 0.000000846 0.0000005263 0.000

lb/mmBtuO2 8.98E-11 6.68E-11 0.000

ng/dscm 1.01E-01 7.96E-02 0.090

ng/dscm@7%O2 1.01E-01 7.50E-02 0.088

Compound: Total Furans

Average

RunNumber 1 2

Friday, February 11, 2011 Page 15 of 32
Dynegy Danskammer Unit 1

Mass_mg 0.000001272 0.000000909 0.000

lb/mmBtuO2 1.35E-10 1.15E-10 0.000

ng/dscm 1.52E-01 1.37E-01 0.145

ng/dscm@7%O2 1.52E-01 1.29E-01 0.141

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2

lb/mmBtuO2 6.96E-05 2.68E-04 0.000

ppm 4.54E-02 1.74E-01 0.110

ppm@7%O2 4.26E-02 1.65E-01 0.104

Location: Stack Exit - Method 26

Compound: Hydrogen Chloride

Average

RunNumber 1 2

Mass_mg 1.9 1.7 1.800

lb/mmBtuO2 8.65E-04 7.86E-04 0.001

mg/dscm 1.03E+00 9.33E-01 0.982

ppm 6.82E-01 6.15E-01 0.649

ppm@7%O2 6.41E-01 5.82E-01 0.612

Compound: Hydrogen Fluoride

Average

RunNumber 1 2

Mass_mg 0.47 0.04 0.255

lb/mmBtuO2 2.14E-04 1.85E-05 0.000

mg/dscm 2.56E-01 2.20E-02 0.139

ppm 3.08E-01 2.64E-02 0.167

ppm@7%O2 2.89E-01 2.50E-02 0.157

Location: Stack Exit - Method 29 

Compound: Antimony

Average

RunNumber 1 2

Mass_mg 0.0055 0.0051 0.005

lb/mmBtuO2 1.38E-06 1.25E-06 0.000

Compound: Arsenic

Average

RunNumber 1 2

Mass_mg 0.0049 0.0045 0.005

lb/mmBtuO2 1.23E-06 1.10E-06 0.000

Compound: Beryllium

Average

RunNumber 1 2

Mass_mg 0.001 0.001 0.001

lb/mmBtuO2 2.51E-07 2.45E-07 0.000

Friday, February 11, 2011 Page 16 of 32
Dynegy Danskammer Unit 1

Compound: Cadmium

Average

RunNumber 1 2

Mass_mg 0.0109 0.00725 0.009

lb/mmBtuO2 2.73E-06 1.78E-06 0.000

Compound: Chromium

Average

RunNumber 1 2

Mass_mg 0.0103 0.0164 0.013

lb/mmBtuO2 2.58E-06 4.03E-06 0.000

Compound: Cobalt

Average

RunNumber 1 2

Mass_mg 0.00401 0.00395 0.004

lb/mmBtuO2 1.00E-06 9.70E-07 0.000

Compound: Filterable Particulate

Average

RunNumber 1 2

Mass_mg 128.5 268.9 198.700

lb/mmBtuO2 3.22E-02 6.60E-02 0.049

Compound: Lead

Average

RunNumber 1 2

Mass_mg 0.0415 0.0411 0.041

lb/mmBtuO2 1.04E-05 1.01E-05 0.000

Compound: Manganese

Average

RunNumber 1 2

Mass_mg 0.031 0.0308 0.031

lb/mmBtuO2 7.77E-06 7.56E-06 0.000

Compound: Nickel

Average

RunNumber 1 2

Mass_mg 0.0988 0.0901 0.094

lb/mmBtuO2 2.48E-05 2.21E-05 0.000

Compound: Selenium

Average

RunNumber 1 2

Mass_mg 0.01 0.0111 0.011

lb/mmBtuO2 2.51E-06 2.73E-06 0.000

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2

lb/mmBtuO2 9.95E-01 9.95E-01 0.995

Friday, February 11, 2011 Page 17 of 32
Dynegy Danskammer Unit 1

Process Run Data

ppm 4.46E+02 4.43E+02 444.500

ppm@7%O2 4.19E+02 4.19E+02 419.000

Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2

lb/mmBtuO2 2.43E-01 2.53E-01 0.248

ppm 1.52E+02 1.57E+02 154.500

ppm@7%O2 1.43E+02 1.48E+02 145.500

Location: Stack Exit - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 1 2

Mass_mg 10.9 7.9 9.400

lb/mmBtuO2 3.88E-03 2.58E-03 0.003

Compound: Filterable PM2.5

Average

RunNumber 1 2

Mass_mg 6.1 5 5.550

lb/mmBtuO2 2.17E-03 1.63E-03 0.002

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2

Mass_mg 114.7 204.7 159.700

lb/mmBtuO2 4.08E-02 6.69E-02 0.054

Compound: Organic Condensible Particulate

Average

RunNumber 1 2

Mass_mg 2.9 10 6.450

lb/mmBtuO2 1.03E-03 3.27E-03 0.002

Compound: Total Particulate

Average

RunNumber 1 2

Mass_mg 128.5 222.6 175.550

lb/mmBtuO2 4.57E-02 7.27E-02 0.059

Compound: Total PM2.5

Average

RunNumber 1 2

Mass_mg 123.7 219.7 171.700

lb/mmBtuO2 4.40E-02 7.18E-02 0.058

Friday, February 11, 2011 Page 18 of 32
Dynegy Danskammer Unit 1

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Average Heat Input 548.32 MMBtu/hr 0

10 Average Heat Input 0 MMBtu/hr 0

11 Average Heat Input 520.44 MMBtu/hr 0

12 Average Heat Input 525.83 MMBtu/hr 0

2 Average Heat Input 524.72 MMBtu/hr 0

3 Average Heat Input 0 MMBtu/hr 0

4 Average Heat Input 519.87 MMBtu/hr 0

5 Average Heat Input 520.58 MMBtu/hr 0

6 Average Heat Input 0 MMBtu/hr 0

7 Average Heat Input 546.85 MMBtu/hr 0

8 Average Heat Input 555.09 MMBtu/hr 0

9 Average Heat Input 0 MMBtu/hr 0

1 Fuel Oil Firing Rate 55.5 gal/min 0

10 Fuel Oil Firing Rate 0 gal/min 0

11 Fuel Oil Firing Rate 54.46 gal/min 0

12 Fuel Oil Firing Rate 54.51 gal/min 0

2 Fuel Oil Firing Rate 54.49 gal/min 0

3 Fuel Oil Firing Rate 0 gal/min 0

4 Fuel Oil Firing Rate 54.43 gal/min 0

5 Fuel Oil Firing Rate 54.46 gal/min 0

6 Fuel Oil Firing Rate 0 gal/min 0

7 Fuel Oil Firing Rate 55.25 gal/min 0

8 Fuel Oil Firing Rate 55.89 gal/min 0

9 Fuel Oil Firing Rate 0 gal/min 0

1 Unit Gross Electrical Output 42.7 Mwe 0 Run 1

10 Unit Gross Electrical Output 0 Mwe 0 Run 3

11 Unit Gross Electrical Output 40.11 Mwe 0 Run 2

12 Unit Gross Electrical Output 40.34 Mwe 0 Run 1

2 Unit Gross Electrical Output 40.34 Mwe 0 Run 2

3 Unit Gross Electrical Output 0 Mwe 0 Run 3

4 Unit Gross Electrical Output 40.32 Mwe 0 Run 1

5 Unit Gross Electrical Output 40.1 Mwe 0 Run 2

6 Unit Gross Electrical Output 0 Mwe 0 Run 3

Friday, February 11, 2011 Page 19 of 32
Dynegy Danskammer Unit 1

APCD Run Data

7 Unit Gross Electrical Output 42.8 Mwe 0 Run 1

8 Unit Gross Electrical Output 42.25 Mwe 0 Run 2

9 Unit Gross Electrical Output 0 Mwe 0 Run 3

1 Opacity 4.56 % Dioxin/Furan 

Organic HAP 

Group

0

10 Opacity 0 % Acid Gas HAP 

Group

0

11 Opacity 3.05 % Acid Gas HAP 

Group

0

12 Opacity 3.27 % Acid Gas HAP 

Group

0

2 Opacity 3.2 % Dioxin/Furan 

Organic HAP 

Group

0

3 Opacity 0 % Dioxin/Furan 

Organic HAP 

Group

0

4 Opacity 3.28 % Non-Dioxin 

Organic HAP 

Group

0

5 Opacity 3.05 % Non-Dioxin 

Organic HAP 

Group

0

6 Opacity 0 % Non-Dioxin 

Organic HAP 

Group

0

7 Opacity 4.97 % Mercury and 

Metallic HAP 

Group

0

8 Opacity 3.87 % Mercury and 

Metallic HAP 

Group

0

9 Opacity 0 % Mercury and 

Metallic HAP 

Group

0

1 Heat Input Million Btus/million BTU using CO2 548.32 0

Run Name Value UOM Comments

Target

Value

1 ELECTROSTATIC PRECIPITATOR 0 kV 0

10 ELECTROSTATIC PRECIPITATOR 0 kV 0

11 ELECTROSTATIC PRECIPITATOR 0 kV 0

12 ELECTROSTATIC PRECIPITATOR 0 kV 0

Friday, February 11, 2011 Page 20 of 32
Dynegy Danskammer Unit 1

Process Lab Run Data

2 ELECTROSTATIC PRECIPITATOR 0 kV 0

3 ELECTROSTATIC PRECIPITATOR 0 kV 0

4 ELECTROSTATIC PRECIPITATOR 0 kV 0

5 ELECTROSTATIC PRECIPITATOR 0 kV 0

6 ELECTROSTATIC PRECIPITATOR 0 kV 0

7 ELECTROSTATIC PRECIPITATOR 0 kV 0

8 ELECTROSTATIC PRECIPITATOR 0 kV 0

9 ELECTROSTATIC PRECIPITATOR 0 kV 0

1 0 0

10 0 0

11 0 0

12 0 0

2 0 0

3 0 0

4 0 0

5 0 0

6 0 0

7 0 0

8 0 0

9 0 0

1 0 0

10 0 0

11 0 0

12 0 0

2 0 0

3 0 0

4 0 0

5 0 0

6 0 0

7 0 0

8 0 0

9 0 0

Run Name Value UOM Comments

1 Moisture As Received 0 %

Friday, February 11, 2011 Page 21 of 32
Dynegy Danskammer Unit 1

2 Moisture As Received 0 %

3 Moisture As Received 0 %

1 Ash As Received 0 %

2 Ash As Received 0 %

3 Ash As Received 0 %

1 Carbon As Received 0 %

2 Carbon As Received 0 %

3 Carbon As Received 0 %

1 Hydrogen (Excl. H in Moisture) As Received 0 %

2 Hydrogen (Excl. H in Moisture) As Received 0 %

3 Hydrogen (Excl. H in Moisture) As Received 0 %

1 Hydrogen (Incl. H in Moisture) As Received 0 %

2 Hydrogen (Incl. H in Moisture) As Received 0 %

3 Hydrogen (Incl. H in Moisture) As Received 0 %

1 Nitrogen AS Received 0 %

2 Nitrogen AS Received 0 %

3 Nitrogen AS Received 0 %

1 Oxygen (Excl. O in Moisture) As Received 0 %

2 Oxygen (Excl. O in Moisture) As Received 0 %

3 Oxygen (Excl. O in Moisture) As Received 0 %

1 Oxygen (Incl. O in Moisture) As Received 0 %

2 Oxygen (Incl. O in Moisture) As Received 0 %

3 Oxygen (Incl. O in Moisture) As Received 0 %

1 Fixed Carbon As Received 0 %

2 Fixed Carbon As Received 0 %

3 Fixed Carbon As Received 0 %

1 Heating Value As Received 0 Btu/lb

2 Heating Value As Received 0 Btu/lb

3 Heating Value As Received 0 Btu/lb

1 Sulfur As Received 0 %

2 Sulfur As Received 0 %

3 Sulfur As Received 0 %

1 Volatile Matter As Received 0 %

2 Volatile Matter As Received 0 %

3 Volatile Matter As Received 0 %

1 Ash Dry Basis 0 %

2 Ash Dry Basis 0 %

3 Ash Dry Basis 0 %

1 Carbon Dry Basis 0 %

2 Carbon Dry Basis 0 %

3 Carbon Dry Basis 0 %

1 Hydrogen (Excl. H in Moisture) Dry Basis 0 %

2 Hydrogen (Excl. H in Moisture) Dry Basis 0 %

Friday, February 11, 2011 Page 22 of 32
Dynegy Danskammer Unit 1

3 Hydrogen (Excl. H in Moisture) Dry Basis 0 %

1 Nitrogen Dry Basis 0 %

2 Nitrogen Dry Basis 0 %

3 Nitrogen Dry Basis 0 %

1 Oxygen (Excl. O in Moisture) Dry Basis 0 %

2 Oxygen (Excl. O in Moisture) Dry Basis 0 %

3 Oxygen (Excl. O in Moisture) Dry Basis 0 %

1 Fixed Carbon Dry Basis 0 %

2 Fixed Carbon Dry Basis 0 %

3 Fixed Carbon Dry Basis 0 %

1 Heating Value Dry Basis 0 Btu/lb

2 Heating Value Dry Basis 0 Btu/lb

3 Heating Value Dry Basis 0 Btu/lb

1 Sulfur Dry Basis 0 %

2 Sulfur Dry Basis 0 %

3 Sulfur Dry Basis 0 %

1 Volatile Matter Dry Basis 0 %

2 Volatile Matter Dry Basis 0 %

3 Volatile Matter Dry Basis 0 %

1 Phosphorus 0 %

1 Antimony 0 %

1 Arenic 0 %

1 Beryllium 0 %

1 Cadmium 0 %

1 Chromium 0 %

1 Cobalt 0 %

1 Lead 0 %

1 Manganese 0 %

1 Nickel 0 %

1 Selenium 0 %

Friday, February 11, 2011 Page 23 of 32
Dynegy Danskammer Unit 1

Sampling / Stack Data Results Detail

Location Stack Exit - Method 0011

Average

Run Number 1 2

Test Date 7/20/2010 7/20/2010

Run Start Time 12:00:00 AM 12:00:00 AM

Run Finish Time 12:14:00 PM 12:59:00 PM

Net Traversing Points 121 121

Net Run Time, minutes 120 120

Nozzle Diameter, inches 0.346 0.346 0.346

Pitot Tube Coefficient 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.992 0.992 0.992

Barometric Pressure, inches of Mercury 29.8 29.8 29.800

Average Orifice Meter Differential, inches H2O 1.45 1.55 1.500

Dry Gas Meter Volume Sampled, cubic feet 80.532 84.118 82.325

Average Dry Gas Meter Temperature, °F 105.86 114.68 110.270

Dry Gas Meter Volume Sampled, dscf 74.509 76.652 75.581

Total Moisture Liquid collected, g 182.1 185.2 183.650

Volume of Water Vapor, standard cubic feet 8.57 8.72 8.645

Moisture Content of Stack Gas, % 10.32 10.21 10.265

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.000

Dry Mole Fraction 0.8968 0.8979 0.897

Carbon Dioxide, % 11.6 11.5 11.550

Oxygen, % 6.1 6.2 6.150

Carbon Monoxide & Nitrogen, % 82.3 82.3 82.300

Fuel Factor 1.28 1.28

Dry Molecular Weight, lb/lb-Mole 30.10 30.09 30.095

Wet Molecular weight, lb/lb-Mole 28.85 28.86 28.855

Flue Gas Static Pressure, inches of H2O -0.32 -0.32 -0.320

Absolute Flue Gas Pressure, inches of Mercury 29.78 29.78 29.780

Average Stack Gas Temperature, °F 297.48 297.22 297.350

Average Velocity Head, inches of H2O 0.1401438284

71915

0.147264536

093235

0.144

Average Stack Gas Velocity, feet/second 25.24 25.87 25.555

Stack Cross-Sectional Area, square feet 113.097 113.097 113.097

Dry Volumetric Flow Rate, dry scfm 106,564.6 109,396.1 107,980.350

Actual Wet Volumetric Flue Gas Flow Rate, acfm 171,274.1 175,549.2 173,411.650

Percent Isokinetic of Sampling Rate, % 100.9 101.1 101.000

Percent Excess Air, % 39.0 39.9 39.450

F-Factor, dscfm/MMBtu @ %O2 9488 9488 9,488.000

Round Duct Diameter, inches 144 144

Rectangular Duct Width, inches 0 0

Rectangular Duct Length, inches 0 0

Fw 0 0 0.000

Fc 0 0 0.000

Friday, February 11, 2011 Page 24 of 32
Dynegy Danskammer Unit 1

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

Friday, February 11, 2011 Page 25 of 32
Dynegy Danskammer Unit 1

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

Friday, February 11, 2011 Page 26 of 32
Dynegy Danskammer Unit 1

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

Friday, February 11, 2011 Page 27 of 32
Dynegy Danskammer Unit 1

Location Stack Exit - Method 26

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

Friday, February 11, 2011 Page 28 of 32
Dynegy Danskammer Unit 1

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

Friday, February 11, 2011 Page 29 of 32
Dynegy Danskammer Unit 1

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

Friday, February 11, 2011 Page 30 of 32
Dynegy Danskammer Unit 1

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

Friday, February 11, 2011 Page 31 of 32
Dynegy Danskammer Unit 1

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

Friday, February 11, 2011 Page 32 of 32