Name: Tim Sisk

Title:

Company: Montville Power, LLC

Sign Date: 8/25/2010

Name: Richard Kopacz

Title: Project Manager

Company: TRC Companies, Inc.

Sign Date: 8/25/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Utility Boiler MACT ICR - Montville Station Unit 5

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.

Wednesday, February 23, 2011 Page 1 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

Facility Information:

Montville Station

74 Lathrop Road

Uncasville CT 06382

Contact: Tim Sisk

Phone: 860-848-6017

Fax:

Email: tim.sisk@nrgenergy.com

Testing Company:

TRC Companies, Inc.

21 Griffin Road North

Windsor CT 06095

Contact:Richard Kopacz

Phone: 860-298-6265

Fax: 860-298-6399

Email: rkopacz@trcsolutions.com

Air Permit Number:

546

Permitted Source ID/Name:

5

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:

Unit 5 is a 955 MMBtu/hr Combustion Engineering tangentially fired boiler capable of producing 81 MW. It is 

equipped with an ESP.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 0901100005 FRS #: 110000316006

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 130.2 0 0 0 1406.2 1236.9 4 3

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Exit Carbon Monoxide Method 10 8 240 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

Wednesday, February 23, 2011 Page 2 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

Stack Exit 1,2,3,4,6,7,8-HpCDD Method 23 3 480 0

Stack Exit OCDD Method 23 3 480 0

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

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

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

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

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

Stack Exit 2,3,4,6,7,8-HxCDF Method 23 3 480 0

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

Stack Exit 1,2,3,4,6,7,8-HpCDF Method 23 3 480 0

Stack Exit 1,2,3,4,7,8,9-HpCDF Method 23 3 480 0

Stack Exit OCDF Method 23 3 480 0

Stack Exit Other TCDD Method 23 0

Stack Exit Other PeCDD Method 23 0

Stack Exit Other HxCDD Method 23 0

Stack Exit Other HpCDD Method 23 0

Stack Exit Other TCDF Method 23 0

Stack Exit Other PeCDF Method 23 0

Stack Exit Other HxCDF Method 23 0

Stack Exit Other HpCDF Method 23 0

Stack Exit Total Dioxins Method 23 3 480 0

Stack Exit Total Furans Method 23 3 480 0

Stack Exit 3,3',4,4'-TCB (PCB77) Method 23 3 480 0

Stack Exit 3,4,4',5-TCB (PCB81) Method 23 3 480 0

Stack Exit 2,3,3',4,4'-PeCB (PCB105) Method 23 3 480 0

Stack Exit 2,3,4,4',5-PeCB (PCB114) Method 23 3 480 0

Stack Exit 2,3',4,4',5-PeCB (PCB118) Method 23 3 480 0

Stack Exit 2',3,4,4',5-PeCB (PCB123) Method 23 3 480 0

Stack Exit 3,3',4,4',5-PeCB (PCB126) Method 23 3 480 0

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

Stack Exit Naphthalene** Method 23 3 480 0

Stack Exit 2-Methylnaphthalene Method 23 3 480 0

Stack Exit Acenaphthylene** Method 23 3 480 0

Stack Exit Acenaphthene** Method 23 3 480 0

Stack Exit Fluorene** Method 23 3 480 0

Stack Exit Phenanthrene** Method 23 3 480 0

Stack Exit Anthracene** Method 23 3 480 0

Stack Exit Fluoranthene** Method 23 3 480 0

Stack Exit Pyrene** Method 23 3 480 0

Stack Exit Benzo(a)Anthracene* Method 23 3 480 0

Stack Exit Chrysene* Method 23 3 480 0

Stack Exit Benzo(b)Fluoranthene* Method 23 3 480 0

Stack Exit Benzo(k)Fluoranthene* Method 23 3 480 0

Stack Exit Benzo(e)Pyrene Method 23 3 480 0

Stack Exit Benzo(a)Pyrene* Method 23 3 480 0

Stack Exit Perylene Method 23 3 480 0

Wednesday, February 23, 2011 Page 3 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

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 Indeno(1,2,3-cd)Pyrene* Method 23 3 480 0

Stack Exit Dibenzo(a,h)Anthracene* Method 23 3 480 0

Stack Exit Benzo(ghi)Perylene** Method 23 3 480 0

Total organic compounds 

(TOC) as Methane

Stack Exit Method 25A 7 240 0

Stack Exit Hydrogen Fluoride Method 26A 3 180 0

Stack Exit Hydrogen Chloride Method 26A 3 180 0

Organic Condensible 

Particulate

Stack Exit OTM - 27/28 3 240 0

Inorganic (Aqueous) 

Condensible Part.

Stack Exit OTM - 27/28 3 240 0

Stack Exit Filterable PM2.5 OTM - 27/28 3 240 0

Stack Exit Selenium Method 29 3 240 0

Stack Exit Filterable Particulate Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Lead Method 29 3 240 0

Stack Exit Antimony Method 29 3 240 0

Stack Exit Arsenic Method 29 3 240 0

Stack Exit Cobalt Method 29 3 240 0

Stack Exit Chromium Method 29 3 240 0

Stack Exit Beryllium Method 29 3 240 0

Stack Exit Cadmium Method 29 3 240 0

Stack Exit Filterable Particulate Method 5 3 120 0

Stack Exit Sulfur Dioxide Method 6C 8 240 0

Stack Exit Nitrogen oxides (NOx) Method 7E 8 240 0

Wednesday, February 23, 2011 Page 4 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

Sampling / Stack Data Results Summary

Location Stack Exit - Method 0011

Average

Run Number 1 2 3

Test Date 2/23/2010 2/23/2010 2/23/2010

Run Start Time

Run Finish Time

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 75.081 74.952 77.302 75.778

Moisture Content of Stack Gas, % 7.91 7.33 7.95 7.730

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

Carbon Dioxide, % 9 9 9 9.000

Oxygen, % 9.2 9.2 9.2 9.200

Average Stack Gas Temperature, °F 310.83 309.83 310.67 310.443

Dry Volumetric Flow Rate, dry scfm 216,737.3 217,892.8 217,247.0 217,292.367

Actual Wet Volumetric Flue Gas Flow Rate, acfm 344,169.4 343,392.7 345,057.0 344,206.367

Percent Isokinetic of Sampling Rate, % 103.0 102.3 105.8 103.700

F-Factor, dscfm/MMBtu @ %O2 9470 9470 9470 9,470.000

Fw 0 0 0 0.000

Fc 0 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

Wednesday, February 23, 2011 Page 5 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

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 10 3 6

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

Wednesday, February 23, 2011 Page 6 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

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

Wednesday, February 23, 2011 Page 7 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

Location Stack Exit - Method 25A 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 25A 3 6

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

Wednesday, February 23, 2011 Page 8 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

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

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

Wednesday, February 23, 2011 Page 9 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

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

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

Wednesday, February 23, 2011 Page 10 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

Location Stack Exit - Method 6C 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 6C 3 6

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

Wednesday, February 23, 2011 Page 11 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

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

Location Stack Exit - Method 7E 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

Wednesday, February 23, 2011 Page 12 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

Location Stack Exit - Method 7E 3 6

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 - 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

Wednesday, February 23, 2011 Page 13 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

Emissions Summary

Location: Stack Exit - Method 0011

Compound: Formaldehyde

Average

RunNumber 1 3 2

Mass_mg 0.004 0.005 0.005 0.005

lb/mmBtuO2 1.99E-06 2.41E-06 2.49E-06 0.000

ppm 1.51E-03 1.83E-03 1.89E-03 0.002

ppm@7%O2 1.79E-03 2.17E-03 2.25E-03 0.002

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 4.04E-03 4.57E-02 6.33E-02 0.038

ppm 3.37E+00 3.84E+01 5.32E+01 31.657

ppm@7%O2 3.90E+00 4.41E+01 6.11E+01 36.367

Location: Stack Exit - Method 10 3

Compound: Carbon Monoxide

Average

Run 4 5 6

lb/mmBtuO2 1.28E-02 1.67E-02 2.85E-02 0.019

ppm 1.03E+01 1.36E+01 2.34E+01 15.767

ppm@7%O2 1.23E+01 1.62E+01 2.76E+01 18.700

Location: Stack Exit - Method 10 3 6

Compound: Carbon Monoxide

Average

Run 7 8

lb/mmBtuO2 1.96E-02 5.32E-03 0.012

ppm 1.59E+01 4.32E+00 10.110

ppm@7%O2 1.89E+01 5.13E+00 12.015

Location: Stack Exit - Method 23

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000951 0.00000018 0.0000001 0.000

lb/mmBtuO2 1.17E-11 2.21E-11 1.26E-11 0.000

ng/dscm 1.13E-02 2.13E-02 1.19E-02 0.015

ng/dscm@7%O2 1.32E-02 2.49E-02 1.41E-02 0.017

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000315 0.000000031 0.000000024 0.000

lb/mmBtuO2 3.89E-12 3.81E-12 3.03E-12 0.000

ng/dscm 3.75E-03 3.67E-03 2.87E-03 0.003

ng/dscm@7%O2 4.38E-03 4.29E-03 3.41E-03 0.004

Wednesday, February 23, 2011 Page 14 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000039 0.0000000036 0.0000000129 0.000

lb/mmBtuO2 4.81E-13 4.42E-13 1.63E-12 0.000

ng/dscm 4.64E-04 4.26E-04 1.54E-03 0.001

ng/dscm@7%O2 5.42E-04 4.98E-04 1.83E-03 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000133 0.000000012 0.000000005 0.000

lb/mmBtuO2 1.64E-12 1.47E-12 6.30E-13 0.000

ng/dscm 1.58E-03 1.42E-03 5.97E-04 0.001

ng/dscm@7%O2 1.85E-03 1.66E-03 7.09E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000093 0.000000013 0.000000013 0.000

lb/mmBtuO2 1.15E-12 1.60E-12 1.64E-12 0.000

ng/dscm 1.11E-03 1.54E-03 1.55E-03 0.001

ng/dscm@7%O2 1.30E-03 1.80E-03 1.84E-03 0.002

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000038 0.0000000236 0.0000000235 0.000

lb/mmBtuO2 4.69E-13 2.90E-12 2.96E-12 0.000

ng/dscm 4.52E-04 2.79E-03 2.81E-03 0.002

ng/dscm@7%O2 5.28E-04 3.26E-03 3.34E-03 0.002

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000082 0.0000000062 0.0000000174 0.000

lb/mmBtuO2 1.01E-12 7.62E-13 2.19E-12 0.000

ng/dscm 9.75E-04 7.34E-04 2.08E-03 0.001

ng/dscm@7%O2 1.14E-03 8.57E-04 2.47E-03 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000039 0.000000021 0.0000000134 0.000

lb/mmBtuO2 4.81E-13 2.58E-12 1.69E-12 0.000

ng/dscm 4.64E-04 2.49E-03 1.60E-03 0.002

ng/dscm@7%O2 5.42E-04 2.91E-03 1.90E-03 0.002

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000052 0.0000000015 0.0000000017 0.000

lb/mmBtuO2 6.42E-13 1.84E-13 2.14E-13 0.000

Wednesday, February 23, 2011 Page 15 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

ng/dscm 6.18E-04 1.78E-04 2.03E-04 0.000

ng/dscm@7%O2 7.22E-04 2.08E-04 2.41E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000028 0.0000000048 0.00000001 0.000

lb/mmBtuO2 3.46E-13 5.90E-13 1.26E-12 0.000

ng/dscm 3.33E-04 5.68E-04 1.19E-03 0.001

ng/dscm@7%O2 3.89E-04 6.63E-04 1.41E-03 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.000000008 0.0000000028 0.0000000029 0.000

lb/mmBtuO2 9.87E-13 3.44E-13 3.66E-13 0.000

ng/dscm 9.51E-04 3.31E-04 3.46E-04 0.001

ng/dscm@7%O2 1.11E-03 3.87E-04 4.11E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000044 0.000000003 0.00000000054 0.000

lb/mmBtuO2 5.43E-13 3.69E-13 6.81E-14 0.000

ng/dscm 5.23E-04 3.55E-04 6.45E-05 0.000

ng/dscm@7%O2 6.11E-04 4.15E-04 7.66E-05 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000699 0.000000069 0.0000000601 0.000

lb/mmBtuO2 8.63E-12 8.48E-12 7.58E-12 0.000

ng/dscm 8.31E-03 8.17E-03 7.18E-03 0.008

ng/dscm@7%O2 9.71E-03 9.54E-03 8.53E-03 0.009

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

Average

RunNumber 1 2 3

Mass_mg 0.000000362 0.000000463 0.00000035 0.000

lb/mmBtuO2 4.47E-11 5.69E-11 4.41E-11 0.000

ng/dscm 4.30E-02 5.48E-02 4.18E-02 0.047

ng/dscm@7%O2 5.02E-02 6.40E-02 4.97E-02 0.055

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

Average

RunNumber 1 2 3

Mass_mg 0.000000019 0.0000000359 0.000000017 0.000

lb/mmBtuO2 2.35E-12 4.41E-12 2.14E-12 0.000

ng/dscm 2.26E-03 4.25E-03 2.03E-03 0.003

ng/dscm@7%O2 2.64E-03 4.96E-03 2.41E-03 0.003

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

Average

RunNumber 1 2 3

Wednesday, February 23, 2011 Page 16 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

Mass_mg 0.000000015 0.000000036 0.000000041 0.000

lb/mmBtuO2 1.85E-12 4.42E-12 5.17E-12 0.000

ng/dscm 1.78E-03 4.26E-03 4.89E-03 0.004

ng/dscm@7%O2 2.08E-03 4.98E-03 5.81E-03 0.004

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

Average

RunNumber 1 2 3

Mass_mg 0.00000119 0.00000153 0.00000142 0.000

lb/mmBtuO2 1.47E-10 1.88E-10 1.79E-10 0.000

ng/dscm 1.41E-01 1.81E-01 1.70E-01 0.164

ng/dscm@7%O2 1.65E-01 2.11E-01 2.02E-01 0.193

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000177 0.0000000083 0.0000000231 0.000

lb/mmBtuO2 2.18E-12 1.02E-12 2.91E-12 0.000

ng/dscm 2.10E-03 9.83E-04 2.76E-03 0.002

ng/dscm@7%O2 2.45E-03 1.15E-03 3.28E-03 0.002

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

Average

RunNumber 1 2 3

Mass_mg 0.000000015 0.000000016 0.000000014 0.000

lb/mmBtuO2 1.85E-12 1.97E-12 1.76E-12 0.000

ng/dscm 1.78E-03 1.89E-03 1.67E-03 0.002

ng/dscm@7%O2 2.08E-03 2.21E-03 1.98E-03 0.002

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000024 0.0000000289 0.0000000019 0.000

lb/mmBtuO2 2.96E-13 3.55E-12 2.40E-13 0.000

ng/dscm 2.85E-04 3.42E-03 2.27E-04 0.001

ng/dscm@7%O2 3.33E-04 3.99E-03 2.70E-04 0.002

Compound: 2,3,7,8-TCDD

Average

RunNumber 1 2 3

Mass_mg 0.000000004 0.0000000054 0.0000000031 0.000

lb/mmBtuO2 4.94E-13 6.64E-13 3.91E-13 0.000

ng/dscm 4.76E-04 6.39E-04 3.70E-04 0.000

ng/dscm@7%O2 5.56E-04 7.46E-04 4.40E-04 0.001

Compound: 2,3,7,8-TCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000035 0.0000000055 0.0000000035 0.000

lb/mmBtuO2 4.32E-13 6.76E-13 4.41E-13 0.000

ng/dscm 4.16E-04 6.51E-04 4.18E-04 0.000

ng/dscm@7%O2 4.86E-04 7.60E-04 4.97E-04 0.001

Wednesday, February 23, 2011 Page 17 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

Compound: 2-Methylnaphthalene

Average

RunNumber 1 2 3

Mass_mg 0.00121 0.0012 0.000862 0.001

lb/mmBtuO2 1.49E-07 1.47E-07 1.09E-07 0.000

ng/dscm 1.44E+02 1.42E+02 1.03E+02 129.667

ng/dscm@7%O2 1.68E+02 1.66E+02 1.22E+02 152.000

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

Average

RunNumber 1 2 3

Mass_mg 0.000000008 0.000000019 0.0000000072 0.000

lb/mmBtuO2 9.87E-13 2.34E-12 9.08E-13 0.000

ng/dscm 9.51E-04 2.25E-03 8.60E-04 0.001

ng/dscm@7%O2 1.11E-03 2.63E-03 1.02E-03 0.002

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000035 0.000000011 0.000000014 0.000

lb/mmBtuO2 4.32E-13 1.35E-12 1.76E-12 0.000

ng/dscm 4.16E-04 1.30E-03 1.67E-03 0.001

ng/dscm@7%O2 4.86E-04 1.52E-03 1.98E-03 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.000000137 0.000000237 0.000000244 0.000

lb/mmBtuO2 1.69E-11 2.91E-11 3.08E-11 0.000

ng/dscm 1.63E-02 2.81E-02 2.91E-02 0.025

ng/dscm@7%O2 1.90E-02 3.28E-02 3.46E-02 0.029

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000071 0.000000021 0.0000000156 0.000

lb/mmBtuO2 8.76E-13 2.58E-12 1.97E-12 0.000

ng/dscm 8.44E-04 2.49E-03 1.86E-03 0.002

ng/dscm@7%O2 9.86E-04 2.91E-03 2.21E-03 0.002

Compound: Acenaphthene**

Average

RunNumber 1 2 3

Mass_mg 0.00023 0.000151 0.000095 0.000

lb/mmBtuO2 2.84E-08 1.86E-08 1.20E-08 0.000

ng/dscm 2.73E+01 1.79E+01 1.13E+01 18.833

ng/dscm@7%O2 3.19E+01 2.09E+01 1.34E+01 22.067

Compound: Acenaphthylene**

Average

RunNumber 1 2 3

Mass_mg 0.0000364 0.0000367 0.0000289 0.000

lb/mmBtuO2 4.49E-09 4.51E-09 3.64E-09 0.000

Wednesday, February 23, 2011 Page 18 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

ng/dscm 4.33E+00 4.34E+00 3.45E+00 4.040

ng/dscm@7%O2 5.06E+00 5.07E+00 4.10E+00 4.743

Compound: Anthracene**

Average

RunNumber 1 2 3

Mass_mg 0.0000449 0.0000648 0.000069 0.000

lb/mmBtuO2 5.54E-09 7.96E-09 8.70E-09 0.000

ng/dscm 5.34E+00 7.67E+00 8.24E+00 7.083

ng/dscm@7%O2 6.24E+00 8.96E+00 9.79E+00 8.330

Compound: Benzo(a)Anthracene*

Average

RunNumber 1 2 3

Mass_mg 0.00000426 0.00000627 0.00000849 0.000

lb/mmBtuO2 5.26E-10 7.71E-10 1.07E-09 0.000

ng/dscm 5.06E-01 7.42E-01 1.01E+00 0.753

ng/dscm@7%O2 5.91E-01 8.67E-01 1.20E+00 0.886

Compound: Benzo(a)Pyrene*

Average

RunNumber 1 2 3

Mass_mg 0.0000024 0.00000168 0.00000248 0.000

lb/mmBtuO2 2.96E-10 2.06E-10 3.13E-10 0.000

ng/dscm 2.85E-01 1.99E-01 2.96E-01 0.260

ng/dscm@7%O2 3.33E-01 2.32E-01 3.52E-01 0.306

Compound: Benzo(b)Fluoranthene*

Average

RunNumber 1 2 3

Mass_mg 0.00000732 0.00000627 0.00000683 0.000

lb/mmBtuO2 9.04E-10 7.71E-10 8.61E-10 0.000

ng/dscm 8.70E-01 7.42E-01 8.15E-01 0.809

ng/dscm@7%O2 1.02E+00 8.67E-01 9.68E-01 0.952

Compound: Benzo(e)Pyrene

Average

RunNumber 1 2 3

Mass_mg 0.00000408 0.00000285 0.0000079 0.000

lb/mmBtuO2 5.04E-10 3.50E-10 9.96E-10 0.000

ng/dscm 4.85E-01 3.37E-01 9.43E-01 0.588

ng/dscm@7%O2 5.67E-01 3.94E-01 1.12E+00 0.694

Compound: Benzo(ghi)Perylene**

Average

RunNumber 1 2 3

Mass_mg 0.000011 0.00000453 0.00000363 0.000

lb/mmBtuO2 1.36E-09 5.57E-10 4.58E-10 0.000

ng/dscm 1.31E+00 5.36E-01 4.33E-01 0.760

ng/dscm@7%O2 1.53E+00 6.26E-01 5.14E-01 0.890

Compound: Benzo(k)Fluoranthene*

Average

RunNumber 1 2 3

Wednesday, February 23, 2011 Page 19 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

Mass_mg 0.00000527 0.00000284 0.00000396 0.000

lb/mmBtuO2 6.50E-10 3.49E-10 4.99E-10 0.000

ng/dscm 6.27E-01 3.36E-01 4.73E-01 0.479

ng/dscm@7%O2 7.32E-01 3.92E-01 5.62E-01 0.562

Compound: Chrysene*

Average

RunNumber 1 2 3

Mass_mg 0.0000136 0.000012 0.0000125 0.000

lb/mmBtuO2 1.68E-09 1.47E-09 1.58E-09 0.000

ng/dscm 1.62E+00 1.42E+00 1.49E+00 1.510

ng/dscm@7%O2 1.89E+00 1.66E+00 1.77E+00 1.773

Compound: Dibenzo(a,h)Anthracene*

Average

RunNumber 1 2 3

Mass_mg 0.0000057 0.0000029 0.0000021 0.000

lb/mmBtuO2 7.04E-10 3.56E-10 2.65E-10 0.000

ng/dscm 6.78E-01 3.43E-01 2.51E-01 0.424

ng/dscm@7%O2 7.92E-01 4.01E-01 2.98E-01 0.497

Compound: Fluoranthene**

Average

RunNumber 1 2 3

Mass_mg 0.000139 0.000189 0.000168 0.000

lb/mmBtuO2 1.72E-08 2.32E-08 2.12E-08 0.000

ng/dscm 1.65E+01 2.24E+01 2.01E+01 19.667

ng/dscm@7%O2 1.93E+01 2.62E+01 2.39E+01 23.133

Compound: Fluorene**

Average

RunNumber 1 2 3

Mass_mg 0.000222 0.000264 0.000284 0.000

lb/mmBtuO2 2.74E-08 3.24E-08 3.58E-08 0.000

ng/dscm 2.64E+01 3.13E+01 3.39E+01 30.533

ng/dscm@7%O2 3.08E+01 3.66E+01 4.03E+01 35.900

Compound: Indeno(1,2,3-cd)Pyrene*

Average

RunNumber 1 2 3

Mass_mg 0.0000076 0.0000044 0.00000347 0.000

lb/mmBtuO2 9.38E-10 5.41E-10 4.37E-10 0.000

ng/dscm 9.04E-01 5.21E-01 4.14E-01 0.613

ng/dscm@7%O2 1.06E+00 6.09E-01 4.92E-01 0.720

Compound: Naphthalene**

Average

RunNumber 1 2 3

Mass_mg 0.00512 0.00393 0.00371 0.004

lb/mmBtuO2 6.32E-07 4.83E-07 4.68E-07 0.000

ng/dscm 6.09E+02 4.65E+02 4.43E+02 505.667

ng/dscm@7%O2 7.11E+02 5.43E+02 5.26E+02 593.333

Wednesday, February 23, 2011 Page 20 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

Compound: OCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000012 0.000000219 0.000000089 0.000

lb/mmBtuO2 1.48E-11 2.69E-11 1.12E-11 0.000

ng/dscm 1.43E-02 2.59E-02 1.06E-02 0.017

ng/dscm@7%O2 1.67E-02 3.03E-02 1.26E-02 0.020

Compound: OCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000057 0.0000000037 0.0000000178 0.000

lb/mmBtuO2 7.04E-13 4.55E-13 2.24E-12 0.000

ng/dscm 6.78E-04 4.38E-04 2.13E-03 0.001

ng/dscm@7%O2 7.92E-04 5.12E-04 2.53E-03 0.001

Compound: Other HpCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000001109 0.00000019 0.000000168 0.000

lb/mmBtuO2 1.37E-11 2.34E-11 2.12E-11 0.000

ng/dscm 1.32E-02 2.25E-02 2.01E-02 0.019

ng/dscm@7%O2 1.54E-02 2.63E-02 2.39E-02 0.022

Compound: Other HpCDF

Average

RunNumber 1 2 3

Mass_mg 0 0 0 0.000

lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

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

Compound: Other HxCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000117 0 0.0000001341 0.000

lb/mmBtuO2 1.44E-12 0.00E+00 1.69E-11 0.000

ng/dscm 1.39E-03 0.00E+00 1.60E-02 0.006

ng/dscm@7%O2 1.62E-03 0.00E+00 1.90E-02 0.007

Compound: Other HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000106 0.0000000476 0 0.000

lb/mmBtuO2 1.31E-12 5.85E-12 0.00E+00 0.000

ng/dscm 1.26E-03 5.64E-03 0.00E+00 0.002

ng/dscm@7%O2 1.47E-03 6.59E-03 0.00E+00 0.003

Compound: Other PeCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000476 0.000000142 0.0000000807 0.000

lb/mmBtuO2 5.88E-12 1.75E-11 1.02E-11 0.000

Wednesday, February 23, 2011 Page 21 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

ng/dscm 5.66E-03 1.68E-02 9.63E-03 0.011

ng/dscm@7%O2 6.61E-03 1.96E-02 1.14E-02 0.013

Compound: Other PeCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000521 0.0000000361 0.000000011 0.000

lb/mmBtuO2 6.43E-12 4.44E-12 1.39E-12 0.000

ng/dscm 6.19E-03 4.27E-03 1.31E-03 0.004

ng/dscm@7%O2 7.23E-03 4.99E-03 1.56E-03 0.005

Compound: Other TCDD

Average

RunNumber 1 2 3

Mass_mg 0 0.0000000553 0 0.000

lb/mmBtuO2 0.00E+00 6.80E-12 0.00E+00 0.000

ng/dscm 0.00E+00 6.55E-03 0.00E+00 0.002

ng/dscm@7%O2 0.00E+00 7.65E-03 0.00E+00 0.003

Compound: Other TCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000119 0 0.00000000513 0.000

lb/mmBtuO2 1.47E-12 0.00E+00 6.47E-13 0.000

ng/dscm 1.41E-03 0.00E+00 6.12E-04 0.001

ng/dscm@7%O2 1.65E-03 0.00E+00 7.27E-04 0.001

Compound: Perylene

Average

RunNumber 1 2 3

Mass_mg 0.0000023 0.000001 0.00000094 0.000

lb/mmBtuO2 2.84E-10 1.23E-10 1.18E-10 0.000

ng/dscm 2.73E-01 1.18E-01 1.12E-01 0.168

ng/dscm@7%O2 3.19E-01 1.38E-01 1.33E-01 0.197

Compound: Phenanthrene**

Average

RunNumber 1 2 3

Mass_mg 0.000851 0.0013 0.0012 0.001

lb/mmBtuO2 1.05E-07 1.60E-07 1.51E-07 0.000

ng/dscm 1.01E+02 1.54E+02 1.43E+02 132.667

ng/dscm@7%O2 1.18E+02 1.80E+02 1.70E+02 156.000

Compound: Pyrene**

Average

RunNumber 1 2 3

Mass_mg 0.000276 0.000211 0.0000825 0.000

lb/mmBtuO2 3.41E-08 2.59E-08 1.04E-08 0.000

ng/dscm 3.28E+01 2.50E+01 9.85E+00 22.550

ng/dscm@7%O2 3.83E+01 2.92E+01 1.17E+01 26.400

Compound: Total Dioxins

Average

RunNumber 1 2 3

Wednesday, February 23, 2011 Page 22 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

Mass_mg 0.0000004131 0.0000008531 0.0000006268 0.000

lb/mmBtuO2 5.10E-11 1.05E-10 7.90E-11 0.000

ng/dscm 4.91E-02 1.01E-01 7.48E-02 0.075

ng/dscm@7%O2 5.74E-02 1.18E-01 8.89E-02 0.088

Compound: Total Furans

Average

RunNumber 1 2 3

Mass_mg 0.0000001673 0.0000001959 0.00000012523 0.000

lb/mmBtuO2 2.06E-11 2.41E-11 1.58E-11 0.000

ng/dscm 1.99E-02 2.32E-02 1.50E-02 0.019

ng/dscm@7%O2 2.32E-02 2.71E-02 1.78E-02 0.023

Compound: Total PCBs

Average

RunNumber 1 2 3

Mass_mg 0.0000018336 0.0000024332 0.00000219254 0.000

lb/mmBtuO2 2.26E-10 2.99E-10 2.76E-10 0.000

ng/dscm 2.18E-01 2.88E-01 2.62E-01 0.256

ng/dscm@7%O2 2.55E-01 3.36E-01 3.11E-01 0.301

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 1.05E-03 9.83E-04 1.35E-03 0.001

ppm 1.53E+00 1.44E+00 1.99E+00 1.653

ppm@7%O2 1.77E+00 1.65E+00 2.29E+00 1.903

Location: Stack Exit - Method 25A 3

Compound: Total organic compounds (TOC) as 

Average

Run 4 5 6

lb/mmBtuO2 1.15E-03 7.77E-04 6.58E-04 0.001

ppm 1.61E+00 1.10E+00 9.42E-01 1.217

ppm@7%O2 1.93E+00 1.31E+00 1.11E+00 1.450

Location: Stack Exit - Method 25A 3 6

Compound: Total organic compounds (TOC) as 

Average

Run 7 8

lb/mmBtuO2 4.61E-04 7.95E-04 0.001

ppm 6.54E-01 1.13E+00 0.892

ppm@7%O2 7.77E-01 1.34E+00 1.059

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 3.1 3.1 2.3 2.833

lb/mmBtuO2 1.01E-03 1.01E-03 7.97E-04 0.001

Wednesday, February 23, 2011 Page 23 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.56 0.52 0.48 0.520

lb/mmBtuO2 1.83E-04 1.69E-04 1.66E-04 0.000

Location: Stack Exit - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.01074 0.01523 0.02053 0.016

lb/mmBtuO2 2.61E-06 3.82E-06 4.99E-06 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.001245 0.00132 0.0014 0.001

lb/mmBtuO2 3.02E-07 3.31E-07 3.40E-07 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.000165 0.00018 0.0002775 0.000

lb/mmBtuO2 4.01E-08 4.51E-08 6.74E-08 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.00009 0.000255 0.0001725 0.000

lb/mmBtuO2 2.19E-08 6.39E-08 4.19E-08 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.00514 0.00659 0.00514 0.006

lb/mmBtuO2 1.25E-06 1.65E-06 1.25E-06 0.000

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.00607 0.00752 0.00965 0.008

lb/mmBtuO2 1.47E-06 1.88E-06 2.35E-06 0.000

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 7.8 7.5 24 13.100

lb/mmBtuO2 1.89E-03 1.88E-03 5.83E-03 0.003

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.0072 0.00721 0.0085 0.008

Wednesday, February 23, 2011 Page 24 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

lb/mmBtuO2 1.75E-06 1.81E-06 2.07E-06 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.0421 0.0244 0.0298 0.032

lb/mmBtuO2 1.02E-05 6.11E-06 7.24E-06 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.07445 0.0919 0.12 0.095

lb/mmBtuO2 1.81E-05 2.30E-05 2.92E-05 0.000

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.0085 0.00115 0.00208 0.004

lb/mmBtuO2 2.06E-06 2.88E-07 5.06E-07 0.000

Location: Stack Exit - Method 5

Compound: Filterable Particulate

Average

RunNumber 1 3 2

Mass_mg 5.2 4.2 4.8 4.733

lb/mmBtuO2 2.62E-03 2.12E-03 2.44E-03 0.002

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

lb/mmBtuO2 3.10E-01 3.12E-01 3.16E-01 0.313

ppm 1.13E+02 1.15E+02 1.16E+02 114.667

ppm@7%O2 1.31E+02 1.32E+02 1.33E+02 132.000

Location: Stack Exit - Method 6C 3

Compound: Sulfur Dioxide

Average

Run 4 5 6

lb/mmBtuO2 3.14E-01 3.19E-01 3.18E-01 0.317

ppm 1.11E+02 1.13E+02 1.14E+02 112.667

ppm@7%O2 1.33E+02 1.34E+02 1.34E+02 133.667

Location: Stack Exit - Method 6C 3 6

Compound: Sulfur Dioxide

Average

Run 7 8

lb/mmBtuO2 3.07E-01 2.99E-01 0.303

ppm 1.09E+02 1.06E+02 107.500

ppm@7%O2 1.29E+02 1.26E+02 127.500

Location: Stack Exit - Method 7E

Wednesday, February 23, 2011 Page 25 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

Process Run Data

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

lb/mmBtuO2 1.41E-01 1.36E-01 1.31E-01 0.136

ppm 7.17E+01 6.95E+01 6.71E+01 69.433

ppm@7%O2 8.31E+01 7.98E+01 7.71E+01 80.000

Location: Stack Exit - Method 7E 3

Compound: Nitrogen oxides (NOx)

Average

Run 4 5 6

lb/mmBtuO2 1.36E-01 1.36E-01 1.33E-01 0.135

ppm 6.68E+01 6.72E+01 6.64E+01 66.800

ppm@7%O2 8.00E+01 7.98E+01 7.82E+01 79.333

Location: Stack Exit - Method 7E 3 6

Compound: Nitrogen oxides (NOx)

Average

Run 7 8

lb/mmBtuO2 1.35E-01 1.40E-01 0.138

ppm 6.70E+01 6.95E+01 68.250

ppm@7%O2 7.96E+01 8.26E+01 81.100

Location: Stack Exit - OTM - 27/28

Compound: Filterable PM2.5

Average

RunNumber 2 3 4

Mass_mg 3 6 2.9 3.967

lb/mmBtuO2 1.21E-03 1.70E-03 1.15E-03 0.001

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 2 3 4

Mass_mg 5.5 5.4 13 7.967

lb/mmBtuO2 2.22E-03 1.53E-03 5.16E-03 0.003

Compound: Organic Condensible Particulate

Average

RunNumber 2 3 4

Mass_mg 2.7 3.5 3.7 3.300

lb/mmBtuO2 1.09E-03 9.92E-04 1.47E-03 0.001

Wednesday, February 23, 2011 Page 26 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input 839.48 Million Btus/hr Collected during 

M23 run 1

0

2 Heat Input 851.19 Million Btus/hr Collected during 

M23 run 2

0

3 Heat Input 812.06 Million Btus/hr Collected during 

M23 run 3

0

1 Steam Output 525 1000 lb steam/hr Collected during 

M23 run 1

0

2 Steam Output 525 1000 lb steam/hr Collected during 

M23 run 2

0

3 Steam Output 525 1000 lb steam/hr Collected during 

M23 run 3

0

1 Fuel Oil Firing Rate 4581.3 gal/hr Collected during 

M23 run 1

0

2 Fuel Oil Firing Rate 4549.1 gal/hr Collected during 

M23 run 2

0

3 Fuel Oil Firing Rate 4576.5 gal/hr Collected during 

M23 run 3

0

1 Flue Gas Flow Rate 1E+07 SCFH Collected during 

M23 run 1

0

1 Flue Gas Carbon Dioxide Content 8.54 % Collected during 

M23 run 1

0

1 Flue Gas Sampling Point Temperature 297 Deg F Collected during 

M23 run 1

0

1 Unit Gross Electrical Output 68.28 MW Collected during 

M23 run 1

0

1 Unit Net Electric Generation 64.28 MW Collected during 

M23 run 1

0

1 Stack Pressure 29.65 in Hg Collected during 

M23 run 1

0

2 Flue Gas Flow Rate 1E+07 SCFH Collected during 

M23 run 2

0

2 Flue Gas Carbon Dioxide Content 8.74 % Collected during 

M23 run 2

0

2 Flue Gas Sampling Point Temperature 306 Deg F Collected during 

M23 run 2

0

2 Unit Gross Electrical Output 67.67 MW Collected during 

M23 run 2

0

2 Unit Net Electric Generation 63.67 MW Collected during 

M23 run 2

0

2 Stack Pressure 29.63 in Hg Collected during 

M23 run 2

0

Wednesday, February 23, 2011 Page 27 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

3 Flue Gas Flow Rate 1E+07 SCFH Collected during 

M23 run 3

0

3 Flue Gas Carbon Dioxide Content 8.29 % Collected during 

M23 run 3

0

3 Flue Gas Sampling Point Temperature 307 Deg F Collected during 

M23 run 3

0

3 Unit Gross Electrical Output 68.16 MW Collected during 

M23 run 3

0

3 Unit Net Electric Generation 64.16 MW Collected during 

M23 run 3

0

3 Stack Pressure 229.67 in Hg Collected during 

M23 run 3

0

1 Flue Gas SO2 Content 106.19 ppm Collected during 

M23 run 1

0

2 Flue Gas SO2 Content 128.97 ppm Collected during 

M23 run 2

0

3 Flue Gas SO2 Content 105.88 ppm Collected during 

M23 run 3

0

1 Flue Gas NOx Content 0.14 lb/MMBtu Collected during 

M23 run 1

0

2 Flue Gas NOx Content 0.15 lb/MMBtu Collected during 

M23 run 2

0

3 Flue Gas NOx Content 0.13 lb/MMBtu Collected during 

M23 run 3

0

4 Heat Input 841.48 Million Btus/hr Collected during 

M29 run 1

0

4 Steam Output 525 1000 lb steam/hr Collected during 

M29 run 1

0

4 Fuel Oil Firing Rate 4589.4 gal/hr Collected during 

M29 run 1

0

4 Flue Gas Flow Rate 1E+07 SCFH Collected during 

M29 run 1

0

4 Flue Gas Carbon Dioxide Content 8.48 % Collected during 

M29 run 1

0

4 Flue Gas Sampling Point Temperature 297 Deg F Collected during 

M29 run 1

0

4 Unit Gross Electrical Output 68.44 MW Collected during 

M29 run 1

0

4 Unit Net Electric Generation 64.44 MW Collected during 

M29 run 1

0

4 Stack Pressure 29.64 in Hg Collected during 

M29 run 1

0

4 Flue Gas SO2 Content 105.04 ppm Collected during 

M29 run 1

0

4 Flue Gas NOx Content 0.14 lb/MMBtu Collected during 

M29 run 1

0

Wednesday, February 23, 2011 Page 28 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

5 Heat Input 834.76 Million Btus/hr Collected during 

M29 run 2

0

5 Steam Output 525 1000 lb steam/hr Collected during 

M29 run 2

0

5 Fuel Oil Firing Rate 4569.1 gal/hr Collected during 

M29 run 2

0

5 Flue Gas Flow Rate 1E+07 SCFH Collected during 

M29 run 2

0

5 Flue Gas Carbon Dioxide Content 8.61 % Collected during 

M29 run 2

0

5 Flue Gas Sampling Point Temperature 299 Deg F Collected during 

M29 run 2

0

5 Unit Gross Electrical Output 68 MW Collected during 

M29 run 2

0

5 Unit Net Electric Generation 64 MW Collected during 

M29 run 2

0

5 Stack Pressure 29.67 in Hg Collected during 

M29 run 2

0

5 Flue Gas SO2 Content 108.01 ppm Collected during 

M29 run 2

0

5 Flue Gas NOx Content 0.13 lb/MMBtu Collected during 

M29 run 2

0

6 Heat Input 875.3 Million Btus/hr Collected during 

M29 run 3

0

6 Steam Output 525 1000 lb steam/hr Collected during 

M29 run 3

0

6 Fuel Oil Firing Rate 4546 gal/hr Collected during 

M29 run 3

0

6 Flue Gas Flow Rate 1E+07 SCFH Collected during 

M29 run 3

0

6 Flue Gas Carbon Dioxide Content 9.12 % Collected during 

M29 run 3

0

6 Flue Gas Sampling Point Temperature 305 Deg F Collected during 

M29 run 3

0

6 Unit Gross Electrical Output 67.58 MW Collected during 

M29 run 3

0

6 Unit Net Electric Generation 63.58 MW Collected during 

M29 run 3

0

6 Stack Pressure 29.61 in Hg Collected during 

M29 run 3

0

6 Flue Gas SO2 Content 147.92 ppm Collected during 

M29 run 3

0

6 Flue Gas NOx Content 0.17 lb/MMBtu Collected during 

M29 run 3

0

Wednesday, February 23, 2011 Page 29 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

7 Heat Input 841.01 Million Btus/hr Collected during 

run 1 of Method 

6C, 7E, 10, and 

25A

0

7 Steam Output 525 1000 lb steam/hr Collected during 

run 1 of Method 

6C, 7E, 10, and 

25A

0

7 Fuel Oil Firing Rate 4580.9 gal/hr Collected during 

run 1 of Method 

6C, 7E, 10, and 

25A

0

7 Flue Gas Flow Rate 1E+07 SCFH Collected during 

run 1 of Method 

6C, 7E, 10, and 

25A

0

7 Flue Gas Carbon Dioxide Content 8.55 % Collected during 

run 1 of Method 

6C, 7E, 10, and 

25A

0

7 Flue Gas Sampling Point Temperature 298 Deg F Collected during 

run 1 of Method 

6C, 7E, 10, and 

25A

0

7 Unit Gross Electrical Output 68.34 MW Collected during 

run 1 of Method 

6C, 7E, 10, and 

25A

0

7 Unit Net Electric Generation 64.34 MW Collected during 

run 1 of Method 

6C, 7E, 10, and 

25A

0

7 Stack Pressure 29.68 in Hg Collected during 

run 1 of Method 

6C, 7E, 10, and 

25A

0

7 Flue Gas SO2 Content 106.44 ppm Collected during 

run 1 of Method 

6C, 7E, 10, and 

25A

0

7 Flue Gas NOx Content 0.14 lb/MMBtu Collected during 

run 1 of Method 

6C, 7E, 10, and 

25A

0

8 Heat Input 834.78 Million Btus/hr Collected during 

run 2 of Method 

6C, 7E, 10, and 

25A

0

Wednesday, February 23, 2011 Page 30 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

8 Steam Output 525 1000 lb steam/hr Collected during 

run 2 of Method 

6C, 7E, 10, and 

25A

0

8 Fuel Oil Firing Rate 4567.3 gal/hr Collected during 

run 2 of Method 

6C, 7E, 10, and 

25A

0

8 Flue Gas Flow Rate 1E+07 SCFH Collected during 

run 2 of Method 

6C, 7E, 10, and 

25A

0

8 Flue Gas Carbon Dioxide Content 8.64 % Collected during 

run 2 of Method 

6C, 7E, 10, and 

25A

0

8 Flue Gas Sampling Point Temperature 300 Deg F Collected during 

run 2 of Method 

6C, 7E, 10, and 

25A

0

8 Unit Gross Electrical Output 67.92 MW Collected during 

run 2 of Method 

6C, 7E, 10, and 

25A

0

8 Unit Net Electric Generation 63.92 MW Collected during 

run 2 of Method 

6C, 7E, 10, and 

25A

0

8 Stack Pressure 29.66 in Hg Collected during 

run 2 of Method 

6C, 7E, 10, and 

25A

0

8 Flue Gas SO2 Content 108.49 ppm Collected during 

run 2 of Method 

6C, 7E, 10, and 

25A

0

8 Flue Gas NOx Content 0.13 lb/MMBtu Collected during 

run 2 of Method 

6C, 7E, 10, and 

25A

0

9 Heat Input 831.94 Million Btus/hr Collected during 

run 3 of Method 

6C, 7E, 10, and 

25A

0

9 Steam Output 525 1000 lb steam/hr Collected during 

run 3 of Method 

6C, 7E, 10, and 

25A

0

Wednesday, February 23, 2011 Page 31 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

9 Fuel Oil Firing Rate 4546.8 gal/hr Collected during 

run 3 of Method 

6C, 7E, 10, and 

25A

0

9 Flue Gas Flow Rate 1E+07 SCFH Collected during 

run 3 of Method 

6C, 7E, 10, and 

25A

0

9 Flue Gas Carbon Dioxide Content 8.73 % Collected during 

run 3 of Method 

6C, 7E, 10, and 

25A

0

9 Flue Gas Sampling Point Temperature 305 Deg F Collected during 

run 3 of Method 

6C, 7E, 10, and 

25A

0

9 Unit Gross Electrical Output 67.63 MW Collected during 

run 3 of Method 

6C, 7E, 10, and 

25A

0

9 Unit Net Electric Generation 63.63 MW Collected during 

run 3 of Method 

6C, 7E, 10, and 

25A

0

9 Stack Pressure 29.61 in Hg Collected during 

run 3 of Method 

6C, 7E, 10, and 

25A

0

9 Flue Gas SO2 Content 119.82 ppm Collected during 

run 3 of Method 

6C, 7E, 10, and 

25A

0

9 Flue Gas NOx Content 0.14 lb/MMBtu Collected during 

run 3 of Method 

6C, 7E, 10, and 

25A

0

10 Heat Input 821.04 Million Btus/hr Collected during 

run 4 of Method 

6C, 7E, 10, and 

25A

0

10 Steam Output 525 1000 lb steam/hr Collected during 

run 4 of Method 

6C, 7E, 10, and 

25A

0

10 Fuel Oil Firing Rate 4552.9 gal/hr Collected during 

run 4 of Method 

6C, 7E, 10, and 

25A

0

Wednesday, February 23, 2011 Page 32 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

10 Flue Gas Flow Rate 1E+07 SCFH Collected during 

run 4 of Method 

6C, 7E, 10, and 

25A

0

10 Flue Gas Carbon Dioxide Content 8.26 % Collected during 

run 4 of Method 

6C, 7E, 10, and 

25A

0

15 Heat Input 834 Million Btus/hr Collected during 

OTM 27/28 run 1

0

15 Steam Output 525 1000 lb steam/hr Collected during 

OTM 27/28 run 1

0

15 Fuel Oil Firing Rate 4569.1 gal/hr Collected during 

OTM 27/28 run 1

0

15 Flue Gas Flow Rate 1E+07 SCFH Collected during 

OTM 27/28 run 1

0

15 Flue Gas Carbon Dioxide Content 8.61 % Collected during 

OTM 27/28 run 1

0

15 Flue Gas Sampling Point Temperature 300 Deg F Collected during 

OTM 27/28 run 1

0

15 Unit Gross Electrical Output 67.98 MW Collected during 

OTM 27/28 run 1

0

15 Unit Net Electric Generation 63.98 MW Collected during 

OTM 27/28 run 1

0

15 Stack Pressure 29.67 in Hg Collected during 

OTM 27/28 run 1

0

15 Flue Gas SO2 Content 108.09 ppm Collected during 

OTM 27/28 run 1

0

15 Flue Gas NOx Content 0.14 lb/MMBtu Collected during 

OTM 27/28 run 1

0

16 Heat Input 865.52 Million Btus/hr Collected during 

OTM 27/28 run 2

0

16 Steam Output 525 1000 lb steam/hr Collected during 

OTM 27/28 run 2

0

16 Fuel Oil Firing Rate 4545.3 gal/hr Collected during 

OTM 27/28 run 2

0

16 Flue Gas Flow Rate 1E+07 SCFH Collected during 

OTM 27/28 run 2

0

16 Flue Gas Carbon Dioxide Content 8.97 % Collected during 

OTM 27/28 run 2

0

16 Flue Gas Sampling Point Temperature 306 Deg F Collected during 

OTM 27/28 run 2

0

16 Unit Gross Electrical Output 67.58 MW Collected during 

OTM 27/28 run 2

0

16 Unit Net Electric Generation 63.58 MW Collected during 

OTM 27/28 run 2

0

Wednesday, February 23, 2011 Page 33 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

16 Stack Pressure 29.61 in Hg Collected during 

OTM 27/28 run 2

0

16 Flue Gas SO2 Content 140.8 ppm Collected during 

OTM 27/28 run 2

0

16 Flue Gas NOx Content 0.16 lb/MMBtu Collected during 

OTM 27/28 run 2

0

17 Heat Input 811.11 Million Btus/hr Collected during 

OTM 27/28 run 3

0

17 Steam Output 525 1000 lb steam/hr Collected during 

OTM 27/28 run 3

0

17 Fuel Oil Firing Rate 4557.3 gal/hr Collected during 

OTM 27/28 run 3

0

17 Flue Gas Flow Rate 1E+07 SCFH Collected during 

OTM 27/28 run 3

0

17 Flue Gas Carbon Dioxide Content 8.31 % Collected during 

OTM 27/28 run 3

0

17 Flue Gas Sampling Point Temperature 305 Deg F Collected during 

OTM 27/28 run 3

0

17 Unit Gross Electrical Output 67.92 MW Collected during 

OTM 27/28 run 3

0

17 Unit Net Electric Generation 63.92 MW Collected during 

OTM 27/28 run 3

0

17 Stack Pressure 29.66 in Hg Collected during 

OTM 27/28 run 3

0

17 Flue Gas SO2 Content 105.84 ppm Collected during 

OTM 27/28 run 3

0

17 Flue Gas NOx Content 0.13 lb/MMBtu Collected during 

OTM 27/28 run 3

0

18 Heat Input 820.82 Million Btus/hr Collected during 

M26A run 1

0

18 Steam Output 525 1000 lb steam/hr Collected during 

M26A run 1

0

18 Fuel Oil Firing Rate 4548.2 gal/hr Collected during 

M26A run 1

0

18 Flue Gas Flow Rate 1E+07 SCFH Collected during 

M26A run 1

0

18 Flue Gas Carbon Dioxide Content 8.26 % Collected during 

M26A run 1

0

18 Flue Gas Sampling Point Temperature 308 Deg F Collected during 

M26A run 1

0

18 Unit Gross Electrical Output 67.7 MW Collected during 

M26A run 1

0

18 Unit Net Electric Generation 63.7 MW Collected during 

M26A run 1

0

18 Stack Pressure 29.64 in Hg Collected during 

M26A run 1

0

Wednesday, February 23, 2011 Page 34 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

18 Flue Gas SO2 Content 105.2 ppm Collected during 

M26A run 1

0

18 Flue Gas NOx Content 0.13 lb/MMBtu Collected during 

M26A run 1

0

19 Heat Input 807.4 Million Btus/hr Collected during 

M26A run 2

0

19 Steam Output 525 1000 lb steam/hr Collected during 

M26A run 2

0

19 Fuel Oil Firing Rate 4565.7 gal/hr Collected during 

M26A run 2

0

19 Flue Gas Flow Rate 1E+07 SCFH Collected during 

M26A run 2

0

19 Flue Gas Carbon Dioxide Content 8.21 % Collected during 

M26A run 2

0

19 Flue Gas Sampling Point Temperature 307 Deg F Collected during 

M26A run 2

0

19 Unit Gross Electrical Output 67.99 MW Collected during 

M26A run 2

0

19 Unit Net Electric Generation 63.99 MW Collected during 

M26A run 2

0

19 Stack Pressure 29.67 in Hg Collected during 

M26A run 2

0

19 Flue Gas SO2 Content 104.54 ppm Collected during 

M26A run 2

0

19 Flue Gas NOx Content 0.13 lb/MMBtu Collected during 

M26A run 2

0

20 Heat Input 820.15 Million Btus/hr Collected during 

M26A run 3

0

20 Steam Output 525 1000 lb steam/hr Collected during 

M26A run 3

0

20 Fuel Oil Firing Rate 4592.9 gal/hr Collected during 

M26A run 3

0

20 Flue Gas Flow Rate 1E+07 SCFH Collected during 

M26A run 3

0

20 Flue Gas Carbon Dioxide Content 8.35 % Collected during 

M26A run 3

0

20 Flue Gas Sampling Point Temperature 307 Deg F Collected during 

M26A run 3

0

20 Unit Gross Electrical Output 68.41 MW Collected during 

M26A run 3

0

20 Unit Net Electric Generation 64.41 MW Collected during 

M26A run 3

0

20 Stack Pressure 29.68 in Hg Collected during 

M26A run 3

0

20 Flue Gas SO2 Content 106.93 ppm Collected during 

M26A run 3

0

Wednesday, February 23, 2011 Page 35 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

20 Flue Gas NOx Content 0.13 lb/MMBtu Collected during 

M26A run 3

0

21 Heat Input 818.66 Million Btus/hr Collected during 

M0011 run 1

0

21 Steam Output 525 1000 lb steam/hr Collected during 

M0011 run 1

0

21 Fuel Oil Firing Rate 4557.2 gal/hr Collected during 

M0011 run 1

0

21 Flue Gas Flow Rate 1E+07 SCFH Collected during 

M0011 run 1

0

21 Flue Gas Carbon Dioxide Content 8.37 % Collected during 

M0011 run 1

0

21 Flue Gas Sampling Point Temperature 305 Deg F Collected during 

M0011 run 1

0

21 Unit Gross Electrical Output 68.13 MW Collected during 

M0011 run 1

0

21 Unit Net Electric Generation 64.13 MW Collected during 

M0011 run 1

0

21 Stack Pressure 29.66 in Hg Collected during 

M0011 run 1

0

21 Flue Gas SO2 Content 105.33 ppm Collected during 

M0011 run 1

0

21 Flue Gas NOx Content 0.13 lb/MMBtu Collected during 

M0011 run 1

0

22 Heat Input 818.35 Million Btus/hr Collected during 

M0011 run 2

0

22 Steam Output 525 1000 lb steam/hr Collected during 

M0011 run 2

0

22 Fuel Oil Firing Rate 4550.7 gal/hr Collected during 

M0011 run 2

0

22 Flue Gas Flow Rate 1E+07 SCFH Collected during 

M0011 run 2

0

22 Flue Gas Carbon Dioxide Content 8.37 % Collected during 

M0011 run 2

0

22 Flue Gas Sampling Point Temperature 305 Deg F Collected during 

M0011 run 2

0

22 Unit Gross Electrical Output 68.15 MW Collected during 

M0011 run 2

0

22 Unit Net Electric Generation 64.15 MW Collected during 

M0011 run 2

0

22 Stack Pressure 29.64 in Hg Collected during 

M0011 run 2

0

22 Flue Gas SO2 Content 105.69 ppm Collected during 

M0011 run 2

0

22 Flue Gas NOx Content 0.13 lb/MMBtu Collected during 

M0011 run 2

0

Wednesday, February 23, 2011 Page 36 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

23 Heat Input 811.78 Million Btus/hr Collected during 

M0011 run 3

0

23 Steam Output 525 1000 lb steam/hr Collected during 

M0011 run 3

0

23 Fuel Oil Firing Rate 4551.6 gal/hr Collected during 

M0011 run 3

0

23 Flue Gas Flow Rate 1E+07 SCFH Collected during 

M0011 run 3

0

23 Flue Gas Carbon Dioxide Content 8.38 % Collected during 

M0011 run 3

0

23 Flue Gas Sampling Point Temperature 305 Deg F Collected during 

M0011 run 3

0

23 Unit Gross Electrical Output 68.2 MW Collected during 

M0011 run 3

0

23 Unit Net Electric Generation 64.2 MW Collected during 

M0011 run 3

0

23 Stack Pressure 29.61 in Hg Collected during 

M0011 run 3

0

23 Flue Gas SO2 Content 105.94 ppm Collected during 

M0011 run 3

0

23 Flue Gas NOx Content 0.13 lb/MMBtu Collected during 

M0011 run 3

0

24 Heat Input 1081.7 Million Btus/hr Collected during 

M5 run 1 retest 

6/4/10

0

24 Steam Output 682.5 1000 lb steam/hr Collected during 

M5 run 1 retest 

6/4/10

0

24 Fuel Oil Firing Rate 5740.1 gal/hr Collected during 

M5 run 1 retest 

6/4/10

0

24 Flue Gas Flow Rate 2E+07 SCFH Collected during 

M5 run 1 retest 

6/4/10

0

24 Flue Gas Carbon Dioxide Content 8.12 % Collected during 

M5 run 1 retest 

6/4/10

0

24 Flue Gas Sampling Point Temperature 229.2 Deg F Collected during 

M5 run 1 retest 

6/4/10

0

24 Unit Gross Electrical Output 87.1 MW Collected during 

M5 run 1 retest 

6/4/10

0

24 Unit Net Electric Generation 83.1 MW Collected during 

M5 run 1 retest 

6/4/10

0

Wednesday, February 23, 2011 Page 37 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

24 Stack Pressure 29.73 in Hg Collected during 

M5 run 1 retest 

6/4/10

0

24 Flue Gas SO2 Content 93.68 ppm Collected during 

M5 run 1 retest 

6/4/10

0

24 Flue Gas NOx Content 0.2 lb/MMBtu Collected during 

M5 run 1 retest 

6/4/10

0

25 Heat Input 1093.5 Million Btus/hr Collected during 

M5 run 2 retest 

6/4/10

0

25 Steam Output 682.5 1000 lb steam/hr Collected during 

M5 run 2 retest 

6/4/10

0

25 Fuel Oil Firing Rate 5811.8 gal/hr Collected during 

M5 run 2 retest 

6/4/10

0

25 Flue Gas Flow Rate 2E+07 SCFH Collected during 

M5 run 2 retest 

6/4/10

0

25 Flue Gas Carbon Dioxide Content 8.17 % Collected during 

M5 run 2 retest 

6/4/10

0

25 Flue Gas Sampling Point Temperature 229.4 Deg F Collected during 

M5 run 2 retest 

6/4/10

0

25 Unit Gross Electrical Output 87.8 MW Collected during 

M5 run 2 retest 

6/4/10

0

25 Unit Net Electric Generation 83.8 MW Collected during 

M5 run 2 retest 

6/4/10

0

25 Stack Pressure 29.72 in Hg Collected during 

M5 run 2 retest 

6/4/10

0

25 Flue Gas SO2 Content 96.4 ppm Collected during 

M5 run 2 retest 

6/4/10

0

25 Flue Gas NOx Content 0.23 lb/MMBtu Collected during 

M5 run 2 retest 

6/4/10

0

26 Heat Input 1087.1 Million Btus/hr Collected during 

M5 run 3 retest 

6/4/10

0

26 Steam Output 682.5 1000 lb steam/hr Collected during 

M5 run 3 retest 

6/4/10

0

Wednesday, February 23, 2011 Page 38 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

26 Fuel Oil Firing Rate 5805.8 gal/hr Collected during 

M5 run 3 retest 

6/4/10

0

26 Flue Gas Flow Rate 2E+07 SCFH Collected during 

M5 run 3 retest 

6/4/10

0

26 Flue Gas Carbon Dioxide Content 8.3 % Collected during 

M5 run 3 retest 

6/4/10

0

26 Flue Gas Sampling Point Temperature 228 Deg F Collected during 

M5 run 3 retest 

6/4/10

0

26 Unit Gross Electrical Output 87.6 MW Collected during 

M5 run 3 retest 

6/4/10

0

26 Unit Net Electric Generation 83.6 MW Collected during 

M5 run 3 retest 

6/4/10

0

26 Stack Pressure 29.71 in Hg Collected during 

M5 run 3 retest 

6/4/10

0

26 Flue Gas SO2 Content 99.93 ppm Collected during 

M5 run 3 retest 

6/4/10

0

26 Flue Gas NOx Content 0.22 lb/MMBtu Collected during 

M5 run 3 retest 

6/4/10

0

10 Flue Gas Sampling Point Temperature 308 Deg F Collected during 

run 4 of Method 

6C, 7E, 10, and 

25A

0

10 Unit Gross Electrical Output 67.77 MW Collected during 

run 4 of Method 

6C, 7E, 10, and 

25A

0

10 Unit Net Electric Generation 63.77 MW Collected during 

run 4 of Method 

6C, 7E, 10, and 

25A

0

10 Stack Pressure 29.64 in Hg Collected during 

run 4 of Method 

6C, 7E, 10, and 

25A

0

10 Flue Gas SO2 Content 105.28 ppm Collected during 

run 4 of Method 

6C, 7E, 10, and 

25A

0

Wednesday, February 23, 2011 Page 39 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

10 Flue Gas NOx Content 0.13 lb/MMBtu Collected during 

run 4 of Method 

6C, 7E, 10, and 

25A

0

11 Heat Input 809.71 Million Btus/hr Collected during 

run 5 of Method 

6C, 7E, 10, and 

25A

0

11 Steam Output 525 1000 lb steam/hr Collected during 

run 5 of Method 

6C, 7E, 10, and 

25A

0

11 Fuel Oil Firing Rate 4573.5 gal/hr Collected during 

run 5 of Method 

6C, 7E, 10, and 

25A

0

11 Flue Gas Flow Rate 1E+07 SCFH Collected during 

run 5 of Method 

6C, 7E, 10, and 

25A

0

11 Flue Gas Carbon Dioxide Content 8.25 % Collected during 

run 5 of Method 

6C, 7E, 10, and 

25A

0

11 Flue Gas Sampling Point Temperature 307 Deg F Collected during 

run 5 of Method 

6C, 7E, 10, and 

25A

0

11 Unit Gross Electrical Output 68.12 MW Collected during 

run 5 of Method 

6C, 7E, 10, and 

25A

0

11 Unit Net Electric Generation 64.12 MW Collected during 

run 5 of Method 

6C, 7E, 10, and 

25A

0

11 Stack Pressure 29.68 in Hg Collected during 

run 5 of Method 

6C, 7E, 10, and 

25A

0

11 Flue Gas SO2 Content 105.27 ppm Collected during 

run 5 of Method 

6C, 7E, 10, and 

25A

0

11 Flue Gas NOx Content 0.13 lb/MMBtu Collected during 

run 5 of Method 

6C, 7E, 10, and 

25A

0

Wednesday, February 23, 2011 Page 40 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

12 Heat Input 814.41 Million Btus/hr Collected during 

run 6 of Method 

6C, 7E, 10, and 

25A

0

12 Steam Output 525 1000 lb steam/hr Collected during 

run 6 of Method 

6C, 7E, 10, and 

25A

0

12 Fuel Oil Firing Rate 4579.4 gal/hr Collected during 

run 6 of Method 

6C, 7E, 10, and 

25A

0

12 Flue Gas Flow Rate 1E+07 SCFH Collected during 

run 6 of Method 

6C, 7E, 10, and 

25A

0

12 Flue Gas Carbon Dioxide Content 8.33 % Collected during 

run 6 of Method 

6C, 7E, 10, and 

25A

0

12 Flue Gas Sampling Point Temperature 306 Deg F Collected during 

run 6 of Method 

6C, 7E, 10, and 

25A

0

12 Unit Gross Electrical Output 68.19 MW Collected during 

run 6 of Method 

6C, 7E, 10, and 

25A

0

12 Unit Net Electric Generation 64.19 MW Collected during 

run 6 of Method 

6C, 7E, 10, and 

25A

0

12 Stack Pressure 29.67 in Hg Collected during 

run 6 of Method 

6C, 7E, 10, and 

25A

0

12 Flue Gas SO2 Content 106.49 ppm Collected during 

run 6 of Method 

6C, 7E, 10, and 

25A

0

12 Flue Gas NOx Content 0.13 lb/MMBtu Collected during 

run 6 of Method 

6C, 7E, 10, and 

25A

0

13 Heat Input 813.87 Million Btus/hr Collected during 

run 7 of Method 

6C, 7E, 10, and 

25A

0

Wednesday, February 23, 2011 Page 41 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

13 Steam Output 525 1000 lb steam/hr Collected during 

run 7 of Method 

6C, 7E, 10, and 

25A

0

13 Fuel Oil Firing Rate 4560.6 gal/hr Collected during 

run 7 of Method 

6C, 7E, 10, and 

25A

0

13 Flue Gas Flow Rate 1E+07 SCFH Collected during 

run 7 of Method 

6C, 7E, 10, and 

25A

0

13 Flue Gas Carbon Dioxide Content 8.35 % Collected during 

run 7 of Method 

6C, 7E, 10, and 

25A

0

13 Flue Gas Sampling Point Temperature 305 Deg F Collected during 

run 7 of Method 

6C, 7E, 10, and 

25A

0

13 Unit Gross Electrical Output 68.03 MW Collected during 

run 7 of Method 

6C, 7E, 10, and 

25A

0

13 Unit Net Electric Generation 64.03 MW Collected during 

run 7 of Method 

6C, 7E, 10, and 

25A

0

13 Stack Pressure 29.66 in Hg Collected during 

run 7 of Method 

6C, 7E, 10, and 

25A

0

13 Flue Gas SO2 Content 105.88 ppm Collected during 

run 7 of Method 

6C, 7E, 10, and 

25A

0

13 Flue Gas NOx Content 0.13 lb/MMBtu Collected during 

run 7 of Method 

6C, 7E, 10, and 

25A

0

14 Heat Input 818.48 Million Btus/hr Collected during 

run 8 of Method 

6C, 7E, 10, and 

25A

0

14 Steam Output 525 1000 lb steam/hr Collected during 

run 8 of Method 

6C, 7E, 10, and 

25A

0

Wednesday, February 23, 2011 Page 42 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

APCD Run Data

Process Lab Run Data

14 Fuel Oil Firing Rate 4553.3 gal/hr Collected during 

run 8 of Method 

6C, 7E, 10, and 

25A

0

14 Flue Gas Flow Rate 1E+07 SCFH Collected during 

run 8 of Method 

6C, 7E, 10, and 

25A

0

14 Flue Gas Carbon Dioxide Content 8.37 % Collected during 

run 8 of Method 

6C, 7E, 10, and 

25A

0

14 Flue Gas Sampling Point Temperature 305 Deg F Collected during 

run 8 of Method 

6C, 7E, 10, and 

25A

0

14 Unit Gross Electrical Output 68.15 MW Collected during 

run 8 of Method 

6C, 7E, 10, and 

25A

0

14 Unit Net Electric Generation 64.15 MW Collected during 

run 8 of Method 

6C, 7E, 10, and 

25A

0

14 Stack Pressure 29.65 in Hg Collected during 

run 8 of Method 

6C, 7E, 10, and 

25A

0

14 Flue Gas SO2 Content 105.56 ppm Collected during 

run 8 of Method 

6C, 7E, 10, and 

25A

0

14 Flue Gas NOx Content 0.13 lb/MMBtu Collected during 

run 8 of Method 

6C, 7E, 10, and 

25A

0

Run Name Value UOM Comments

Target

Value

1 ELECTROSTATIC PRECIPITATOR 0 0

Wednesday, February 23, 2011 Page 43 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

Sampling / Stack Data Results Detail

Location Stack Exit - Method 0011

Average

Run Number 1 2 3

Test Date 2/23/2010 2/23/2010 2/23/2010

Run Start Time

Run Finish Time

Net Traversing Points 12 12 12

Net Run Time, minutes 120 120 120

Nozzle Diameter, inches 0.218 0.218 0.218 0.218

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.989 0.989 0.989 0.989

Barometric Pressure, inches of Mercury 29.93 29.93 29.93 29.930

Average Orifice Meter Differential, inches H2O 1.17 1.17 1.18 1.173

Dry Gas Meter Volume Sampled, cubic feet 76.288 76.264 77.885 76.812

Average Dry Gas Meter Temperature, °F 72.29 73.04 67.83 71.053

Dry Gas Meter Volume Sampled, dscf 75.081 74.952 77.302 75.778

Total Moisture Liquid collected, g 137 126 142 135.000

Volume of Water Vapor, standard cubic feet 6.45 5.93 6.68 6.353

Moisture Content of Stack Gas, % 7.91 7.33 7.95 7.730

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

Dry Mole Fraction 0.9209 0.9267 0.9205 0.923

Carbon Dioxide, % 9 9 9 9.000

Oxygen, % 9.2 9.2 9.2 9.200

Carbon Monoxide & Nitrogen, % 81.8 81.8 81.8 81.800

Fuel Factor 1.30 1.30 1.30

Dry Molecular Weight, lb/lb-Mole 29.81 29.81 29.81 29.810

Wet Molecular weight, lb/lb-Mole 28.88 28.94 28.87 28.897

Flue Gas Static Pressure, inches of H2O -0.87 -0.84 -0.85 -0.853

Absolute Flue Gas Pressure, inches of Mercury 29.87 29.87 29.87 29.870

Average Stack Gas Temperature, °F 310.83 309.83 310.67 310.443

Average Velocity Head, inches of H2O 0.8353076333

48512

0.834283485

345891

0.839448747

593627

0.836

Average Stack Gas Velocity, feet/second 62.04 61.90 62.20 62.047

Stack Cross-Sectional Area, square feet 92.459 92.459 92.459 92.459

Dry Volumetric Flow Rate, dry scfm 216,737.3 217,892.8 217,247.0 217,292.367

Actual Wet Volumetric Flue Gas Flow Rate, acfm 344,169.4 343,392.7 345,057.0 344,206.367

Percent Isokinetic of Sampling Rate, % 103.0 102.3 105.8 103.700

Percent Excess Air, % 74.2 74.2 74.2 74.200

F-Factor, dscfm/MMBtu @ %O2 9470 9470 9470 9,470.000

Round Duct Diameter, inches 130.2 130.2 130.2

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

Wednesday, February 23, 2011 Page 44 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

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

Wednesday, February 23, 2011 Page 45 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

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

Wednesday, February 23, 2011 Page 46 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

Location Stack Exit - Method 10 3 6

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

Wednesday, February 23, 2011 Page 47 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

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

Wednesday, February 23, 2011 Page 48 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

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

Wednesday, February 23, 2011 Page 49 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

Location Stack Exit - Method 25A 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

Wednesday, February 23, 2011 Page 50 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

Location Stack Exit - Method 25A 3 6

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

Wednesday, February 23, 2011 Page 51 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

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

Wednesday, February 23, 2011 Page 52 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

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

Wednesday, February 23, 2011 Page 53 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

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

Wednesday, February 23, 2011 Page 54 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

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

Wednesday, February 23, 2011 Page 55 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

Location Stack Exit - Method 6C 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

Wednesday, February 23, 2011 Page 56 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

Location Stack Exit - Method 6C 3 6

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

Wednesday, February 23, 2011 Page 57 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

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

Wednesday, February 23, 2011 Page 58 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

Location Stack Exit - Method 7E 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

Wednesday, February 23, 2011 Page 59 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

Location Stack Exit - Method 7E 3 6

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

Wednesday, February 23, 2011 Page 60 of 61
Utility Boiler MACT ICR - Montville Station Unit 5

8/25/2010

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

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Wednesday, February 23, 2011 Page 61 of 61