Name: Robert Spooner

Title: Environmental Engineer

Company: Middletown Power, LLC

Sign Date: 7/26/2010

Name: Richard Kopacz

Title: Project Manager

Company: TRC Companies, Inc.

Sign Date: 7/26/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Utility Boiler MACT ICR - Middletown Power Station Unit 2

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.

Sunday, January 30, 2011 Page 1 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

Facility Information:

Middletown Power Station

1866 River Road

Middletown CT 06457

Contact: Robert Spooner

Phone: 860-346-9639

Fax:

Email: bob.spooner@middletownpower.co

m

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:

562

Permitted Source ID/Name:

2

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 2 is a 1064 MMBtu/hr Riley Stoker Corporation dry bottom, front firing oil fired boiler with overfire air, low 

excess air, HERT (SNCR with urea injection) and an ESP.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 0900700108 FRS #: 110000316266

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 178.6 0 0 0 1447 964 4 5

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

Sunday, January 30, 2011 Page 2 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

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 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

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

Sunday, January 30, 2011 Page 3 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

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 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 3 180 0

Stack Exit Hydrogen Fluoride Method 26A 3 180 0

Stack Exit Hydrogen Chloride Method 26A 3 180 0

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

Inorganic (Aqueous) 

Condensible Part.

Stack Exit OTM - 27/28 3 240 0

Organic Condensible 

Particulate

Stack Exit OTM - 27/28 3 240 0

Stack Exit Beryllium Method 29 3 240 0

Stack Exit Selenium 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 Chromium Method 29 3 240 0

Stack Exit Cadmium Method 29 3 240 0

Stack Exit Filterable Particulate Method 29 3 240 0

Stack Exit Cobalt Method 29 3 240 0

Stack Exit Sulfur Dioxide Method 6C 3 180 0

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

Sunday, January 30, 2011 Page 4 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

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Sampling / Stack Data Results Summary

Location Stack Exit - Method 0011

Average

Run Number 1 2 3

Test Date 2/25/2010 2/25/2010 2/25/2010

Run Start Time

Run Finish Time

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 84.661 82.648 81.462 82.924

Moisture Content of Stack Gas, % 11.16 11.04 11.82 11.340

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

Carbon Dioxide, % 10.4 10.4 10.4 10.400

Oxygen, % 7.3 7.3 7.3 7.300

Average Stack Gas Temperature, °F 266.75 267.55 269.10 267.800

Dry Volumetric Flow Rate, dry scfm 154,480.7 150,805.9 149,365.4 151,550.667

Actual Wet Volumetric Flue Gas Flow Rate, acfm 239,982.5 234,136.9 234,450.1 236,189.833

Percent Isokinetic of Sampling Rate, % 104.1 104.1 103.6 103.933

F-Factor, dscfm/MMBtu @ %O2 9420 9420 9420 9,420.000

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

Sunday, January 30, 2011 Page 5 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

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

Sunday, January 30, 2011 Page 6 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

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

Sunday, January 30, 2011 Page 7 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

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

Sunday, January 30, 2011 Page 8 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

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

Sunday, January 30, 2011 Page 9 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

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 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

Sunday, January 30, 2011 Page 10 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

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

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

Sunday, January 30, 2011 Page 11 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

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

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

Sunday, January 30, 2011 Page 12 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

Location Stack Exit - OTM - 27/28

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Sunday, January 30, 2011 Page 13 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

Emissions Summary

Location: Stack Exit - Method 0011

Compound: Formaldehyde

Average

RunNumber 1 2 3

Mass_mg 0.005 0.005 0.004 0.005

lb/mmBtuO2 1.88E-06 1.93E-06 1.57E-06 0.000

ppm 1.67E-03 1.71E-03 1.39E-03 0.002

ppm@7%O2 1.71E-03 1.75E-03 1.42E-03 0.002

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 1.18E-02 2.17E-02 1.80E-02 0.017

ppm 1.11E+01 2.08E+01 1.69E+01 16.267

ppm@7%O2 1.15E+01 2.11E+01 1.75E+01 16.700

Location: Stack Exit - Method 10 3

Compound: Carbon Monoxide

Average

Run 4 5 6

lb/mmBtuO2 1.87E-02 2.55E-02 2.80E-02 0.024

ppm 1.75E+01 2.42E+01 2.68E+01 22.833

ppm@7%O2 1.82E+01 2.47E+01 2.72E+01 23.367

Location: Stack Exit - Method 10 3 6

Compound: Carbon Monoxide

Average

Run 7

lb/mmBtuO2 3.83E-02 0.038

ppm 3.67E+01 36.700

ppm@7%O2 3.70E+01 37.000

Location: Stack Exit - Method 23

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

Average

RunNumber 1 2 3

Mass_mg 0.000000026 0.000000031 0.000000039 0.000

lb/mmBtuO2 2.57E-12 3.15E-12 3.98E-12 0.000

ng/dscm 2.83E-03 3.49E-03 4.40E-03 0.004

ng/dscm@7%O2 2.91E-03 3.57E-03 4.50E-03 0.004

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

Average

RunNumber 1 2 3

Mass_mg 0.000000029 0.000000061 0.000000246 0.000

lb/mmBtuO2 2.87E-12 6.20E-12 2.51E-11 0.000

ng/dscm 3.15E-03 6.86E-03 2.78E-02 0.013

ng/dscm@7%O2 3.24E-03 7.01E-03 2.84E-02 0.013

Sunday, January 30, 2011 Page 14 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000049 0.0000000035 0.0000000027 0.000

lb/mmBtuO2 4.85E-13 3.56E-13 2.75E-13 0.000

ng/dscm 5.33E-04 3.94E-04 3.05E-04 0.000

ng/dscm@7%O2 5.49E-04 4.03E-04 3.12E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000045 0.0000000026 0.0000000037 0.000

lb/mmBtuO2 4.45E-13 2.64E-13 3.78E-13 0.000

ng/dscm 4.89E-04 2.93E-04 4.18E-04 0.000

ng/dscm@7%O2 5.03E-04 2.99E-04 4.27E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000032 0.000000012 0.000000003 0.000

lb/mmBtuO2 3.17E-13 1.22E-12 3.06E-13 0.000

ng/dscm 3.48E-04 1.35E-03 3.39E-04 0.001

ng/dscm@7%O2 3.58E-04 1.38E-03 3.46E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000044 0.0000000025 0.0000000036 0.000

lb/mmBtuO2 4.35E-13 2.54E-13 3.67E-13 0.000

ng/dscm 4.78E-04 2.81E-04 4.06E-04 0.000

ng/dscm@7%O2 4.92E-04 2.87E-04 4.15E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.000000003 0.0000000019 0.000000011 0.000

lb/mmBtuO2 2.97E-13 1.93E-13 1.12E-12 0.000

ng/dscm 3.26E-04 2.14E-04 1.24E-03 0.001

ng/dscm@7%O2 3.36E-04 2.19E-04 1.27E-03 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000046 0.0000000026 0.0000000037 0.000

lb/mmBtuO2 4.55E-13 2.64E-13 3.78E-13 0.000

ng/dscm 5.00E-04 2.93E-04 4.18E-04 0.000

ng/dscm@7%O2 5.15E-04 2.99E-04 4.27E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000034 0.0000000021 0.0000000032 0.000

lb/mmBtuO2 3.36E-13 2.14E-13 3.26E-13 0.000

Sunday, January 30, 2011 Page 15 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

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ng/dscm 3.70E-04 2.36E-04 3.61E-04 0.000

ng/dscm@7%O2 3.81E-04 2.41E-04 3.69E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.000000004 0.0000000045 0.0000000025 0.000

lb/mmBtuO2 3.96E-13 4.58E-13 2.55E-13 0.000

ng/dscm 4.35E-04 5.06E-04 2.82E-04 0.000

ng/dscm@7%O2 4.48E-04 5.17E-04 2.88E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000025 0.0000000035 0.0000000027 0.000

lb/mmBtuO2 2.47E-13 3.56E-13 2.75E-13 0.000

ng/dscm 2.72E-04 3.94E-04 3.05E-04 0.000

ng/dscm@7%O2 2.80E-04 4.03E-04 3.12E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000522 0.000000178 0.000000151 0.000

lb/mmBtuO2 5.17E-12 1.81E-11 1.54E-11 0.000

ng/dscm 5.67E-03 2.00E-02 1.71E-02 0.014

ng/dscm@7%O2 5.84E-03 2.04E-02 1.75E-02 0.015

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

Average

RunNumber 1 2 3

Mass_mg 0.0000001639 0.000000266 0.000000171 0.000

lb/mmBtuO2 1.62E-11 2.70E-11 1.74E-11 0.000

ng/dscm 1.78E-02 2.99E-02 1.93E-02 0.022

ng/dscm@7%O2 1.83E-02 3.06E-02 1.97E-02 0.023

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

Average

RunNumber 1 2 3

Mass_mg 0.000000837 0.00000096 0.000000587 0.000

lb/mmBtuO2 8.28E-11 9.76E-11 5.99E-11 0.000

ng/dscm 9.10E-02 1.08E-01 6.63E-02 0.088

ng/dscm@7%O2 9.37E-02 1.10E-01 6.78E-02 0.091

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

Average

RunNumber 1 2 3

Mass_mg 0.00000005 0.00000008 0.000000045 0.000

lb/mmBtuO2 4.95E-12 8.14E-12 4.59E-12 0.000

ng/dscm 5.43E-03 9.00E-03 5.08E-03 0.007

ng/dscm@7%O2 5.59E-03 9.20E-03 5.19E-03 0.007

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

Average

RunNumber 1 2 3

Sunday, January 30, 2011 Page 16 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

Mass_mg 0.0000000531 0.000000105 0.000000048 0.000

lb/mmBtuO2 5.25E-12 1.07E-11 4.90E-12 0.000

ng/dscm 5.77E-03 1.18E-02 5.42E-03 0.008

ng/dscm@7%O2 5.94E-03 1.21E-02 5.54E-03 0.008

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

Average

RunNumber 1 2 3

Mass_mg 0.0000025 0.00000279 0.00000173 0.000

lb/mmBtuO2 2.47E-10 2.84E-10 1.77E-10 0.000

ng/dscm 2.72E-01 3.14E-01 1.95E-01 0.260

ng/dscm@7%O2 2.80E-01 3.21E-01 1.99E-01 0.267

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000565 0.0000000752 0.000000062 0.000

lb/mmBtuO2 5.59E-12 7.65E-12 6.33E-12 0.000

ng/dscm 6.14E-03 8.46E-03 7.00E-03 0.007

ng/dscm@7%O2 6.32E-03 8.65E-03 7.15E-03 0.007

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

Average

RunNumber 1 2 3

Mass_mg 0.000000003 0.000000012 0.00000002 0.000

lb/mmBtuO2 2.97E-13 1.22E-12 2.04E-12 0.000

ng/dscm 3.26E-04 1.35E-03 2.26E-03 0.001

ng/dscm@7%O2 3.36E-04 1.38E-03 2.31E-03 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000023 0.0000000324 0.0000000026 0.000

lb/mmBtuO2 2.28E-13 3.29E-12 2.65E-13 0.000

ng/dscm 2.50E-04 3.65E-03 2.94E-04 0.001

ng/dscm@7%O2 2.57E-04 3.73E-03 3.00E-04 0.001

Compound: 2,3,7,8-TCDD

Average

RunNumber 1 2 3

Mass_mg 0.000000005 0.0000000047 0.0000000051 0.000

lb/mmBtuO2 4.95E-13 4.78E-13 5.20E-13 0.000

ng/dscm 5.43E-04 5.29E-04 5.76E-04 0.001

ng/dscm@7%O2 5.59E-04 5.41E-04 5.89E-04 0.001

Compound: 2,3,7,8-TCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000047 0.0000000049 0.0000000036 0.000

lb/mmBtuO2 4.65E-13 4.98E-13 3.67E-13 0.000

ng/dscm 5.11E-04 5.51E-04 4.06E-04 0.000

ng/dscm@7%O2 5.26E-04 5.63E-04 4.15E-04 0.001

Sunday, January 30, 2011 Page 17 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

Compound: 2-Methylnaphthalene

Average

RunNumber 1 2 3

Mass_mg 0.00232 0.00176 0.00114 0.002

lb/mmBtuO2 2.30E-07 1.79E-07 1.16E-07 0.000

ng/dscm 2.52E+02 1.98E+02 1.29E+02 193.000

ng/dscm@7%O2 2.59E+02 2.02E+02 1.32E+02 197.667

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

Average

RunNumber 1 2 3

Mass_mg 0.00000003 0.000000146 0.000000303 0.000

lb/mmBtuO2 2.97E-12 1.48E-11 3.09E-11 0.000

ng/dscm 3.26E-03 1.64E-02 3.42E-02 0.018

ng/dscm@7%O2 3.36E-03 1.68E-02 3.50E-02 0.018

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

Average

RunNumber 1 2 3

Mass_mg 0.000000025 0.0000002 0.00000026 0.000

lb/mmBtuO2 2.47E-12 2.03E-11 2.65E-11 0.000

ng/dscm 2.72E-03 2.25E-02 2.94E-02 0.018

ng/dscm@7%O2 2.80E-03 2.30E-02 3.00E-02 0.019

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

Average

RunNumber 1 2 3

Mass_mg 0.000000185 0.000000763 0.00000027 0.000

lb/mmBtuO2 1.83E-11 7.76E-11 2.75E-11 0.000

ng/dscm 2.01E-02 8.59E-02 3.05E-02 0.046

ng/dscm@7%O2 2.07E-02 8.78E-02 3.12E-02 0.047

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

Average

RunNumber 1 2 3

Mass_mg 0.000000032 0.00000013 0.000000096 0.000

lb/mmBtuO2 3.17E-12 1.32E-11 9.79E-12 0.000

ng/dscm 3.48E-03 1.46E-02 1.08E-02 0.010

ng/dscm@7%O2 3.58E-03 1.49E-02 1.10E-02 0.010

Compound: Acenaphthene**

Average

RunNumber 1 2 3

Mass_mg 0.00027 0.00032 0.00075 0.000

lb/mmBtuO2 2.67E-08 3.25E-08 7.65E-08 0.000

ng/dscm 2.93E+01 3.60E+01 8.47E+01 50.000

ng/dscm@7%O2 3.02E+01 3.68E+01 8.66E+01 51.200

Compound: Acenaphthylene**

Average

RunNumber 1 2 3

Mass_mg 0.0000491 0.0000592 0.0000466 0.000

lb/mmBtuO2 4.86E-09 6.02E-09 4.75E-09 0.000

Sunday, January 30, 2011 Page 18 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

ng/dscm 5.34E+00 6.66E+00 5.26E+00 5.753

ng/dscm@7%O2 5.50E+00 6.81E+00 5.38E+00 5.897

Compound: Anthracene**

Average

RunNumber 1 2 3

Mass_mg 0.000028 0.0000871 0.0000602 0.000

lb/mmBtuO2 2.77E-09 8.86E-09 6.14E-09 0.000

ng/dscm 3.04E+00 9.80E+00 6.80E+00 6.547

ng/dscm@7%O2 3.13E+00 1.00E+01 6.95E+00 6.693

Compound: Benzo(a)Anthracene*

Average

RunNumber 1 2 3

Mass_mg 0.0000171 0.0000338 0.000139 0.000

lb/mmBtuO2 1.69E-09 3.44E-09 1.42E-08 0.000

ng/dscm 1.86E+00 3.80E+00 1.57E+01 7.120

ng/dscm@7%O2 1.92E+00 3.88E+00 1.60E+01 7.267

Compound: Benzo(a)Pyrene*

Average

RunNumber 1 2 3

Mass_mg 0.00001 0.0000158 0.0000939 0.000

lb/mmBtuO2 9.89E-10 1.61E-09 9.58E-09 0.000

ng/dscm 1.09E+00 1.78E+00 1.06E+01 4.490

ng/dscm@7%O2 1.12E+00 1.82E+00 1.08E+01 4.580

Compound: Benzo(b)Fluoranthene*

Average

RunNumber 1 2 3

Mass_mg 0.000025 0.0000398 0.000204 0.000

lb/mmBtuO2 2.47E-09 4.05E-09 2.08E-08 0.000

ng/dscm 2.72E+00 4.48E+00 2.30E+01 10.067

ng/dscm@7%O2 2.80E+00 4.58E+00 2.35E+01 10.293

Compound: Benzo(e)Pyrene

Average

RunNumber 1 2 3

Mass_mg 0.0000155 0.0000201 0.000116 0.000

lb/mmBtuO2 1.53E-09 2.04E-09 1.18E-08 0.000

ng/dscm 1.68E+00 2.26E+00 1.31E+01 5.680

ng/dscm@7%O2 1.73E+00 2.31E+00 1.34E+01 5.813

Compound: Benzo(ghi)Perylene**

Average

RunNumber 1 2 3

Mass_mg 0.0000178 0.000027 0.000107 0.000

lb/mmBtuO2 1.76E-09 2.75E-09 1.09E-08 0.000

ng/dscm 1.93E+00 3.04E+00 1.21E+01 5.690

ng/dscm@7%O2 1.99E+00 3.11E+00 1.24E+01 5.833

Compound: Benzo(k)Fluoranthene*

Average

RunNumber 1 2 3

Sunday, January 30, 2011 Page 19 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

Mass_mg 0.0000116 0.000017 0.0000941 0.000

lb/mmBtuO2 1.15E-09 1.73E-09 9.60E-09 0.000

ng/dscm 1.26E+00 1.91E+00 1.06E+01 4.590

ng/dscm@7%O2 1.30E+00 1.95E+00 1.08E+01 4.683

Compound: Chrysene*

Average

RunNumber 1 2 3

Mass_mg 0.0000557 0.000075 0.000199 0.000

lb/mmBtuO2 5.51E-09 7.63E-09 2.03E-08 0.000

ng/dscm 6.05E+00 8.44E+00 2.25E+01 12.330

ng/dscm@7%O2 6.23E+00 8.63E+00 2.30E+01 12.620

Compound: Dibenzo(a,h)Anthracene*

Average

RunNumber 1 2 3

Mass_mg 0.0000057 0.0000073 0.0000283 0.000

lb/mmBtuO2 5.64E-10 7.42E-10 2.89E-09 0.000

ng/dscm 6.20E-01 8.22E-01 3.20E+00 1.547

ng/dscm@7%O2 6.38E-01 8.40E-01 3.27E+00 1.583

Compound: Fluoranthene**

Average

RunNumber 1 2 3

Mass_mg 0.000206 0.000378 0.00054 0.000

lb/mmBtuO2 2.04E-08 3.84E-08 5.51E-08 0.000

ng/dscm 2.24E+01 4.25E+01 6.10E+01 41.967

ng/dscm@7%O2 2.31E+01 4.34E+01 6.23E+01 42.933

Compound: Fluorene**

Average

RunNumber 1 2 3

Mass_mg 0.000221 0.000345 0.000218 0.000

lb/mmBtuO2 2.19E-08 3.51E-08 2.22E-08 0.000

ng/dscm 2.40E+01 3.88E+01 2.46E+01 29.133

ng/dscm@7%O2 2.47E+01 3.97E+01 2.51E+01 29.833

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

Average

RunNumber 1 2 3

Mass_mg 0.0000125 0.0000206 0.000117 0.000

lb/mmBtuO2 1.24E-09 2.09E-09 1.19E-08 0.000

ng/dscm 1.36E+00 2.32E+00 1.32E+01 5.627

ng/dscm@7%O2 1.40E+00 2.37E+00 1.35E+01 5.757

Compound: Naphthalene**

Average

RunNumber 1 2 3

Mass_mg 0.00738 0.00616 0.00496 0.006

lb/mmBtuO2 7.30E-07 6.26E-07 5.06E-07 0.000

ng/dscm 8.02E+02 6.93E+02 5.60E+02 685.000

ng/dscm@7%O2 8.26E+02 7.08E+02 5.72E+02 702.000

Sunday, January 30, 2011 Page 20 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

Compound: OCDD

Average

RunNumber 1 2 3

Mass_mg 0.000000098 0.0000001 0.000000084 0.000

lb/mmBtuO2 9.70E-12 1.02E-11 8.57E-12 0.000

ng/dscm 1.07E-02 1.13E-02 9.48E-03 0.010

ng/dscm@7%O2 1.10E-02 1.15E-02 9.69E-03 0.011

Compound: OCDF

Average

RunNumber 1 2 3

Mass_mg 0.000000003 0.000000014 0.000000028 0.000

lb/mmBtuO2 2.97E-13 1.42E-12 2.86E-12 0.000

ng/dscm 3.26E-04 1.58E-03 3.16E-03 0.002

ng/dscm@7%O2 3.36E-04 1.61E-03 3.23E-03 0.002

Compound: Other HpCDD

Average

RunNumber 1 2 3

Mass_mg 0 0 0.0000000881 0.000

lb/mmBtuO2 0.00E+00 0.00E+00 8.99E-12 0.000

ng/dscm 0.00E+00 0.00E+00 9.95E-03 0.003

ng/dscm@7%O2 0.00E+00 0.00E+00 1.02E-02 0.003

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 0.0000000229 0 0.000

lb/mmBtuO2 0.00E+00 2.33E-12 0.00E+00 0.000

ng/dscm 0.00E+00 2.58E-03 0.00E+00 0.001

ng/dscm@7%O2 0.00E+00 2.64E-03 0.00E+00 0.001

Compound: Other HxCDF

Average

RunNumber 1 2 3

Mass_mg 0 0.000000077 0.000000132 0.000

lb/mmBtuO2 0.00E+00 7.83E-12 1.35E-11 0.000

ng/dscm 0.00E+00 8.67E-03 1.49E-02 0.008

ng/dscm@7%O2 0.00E+00 8.86E-03 1.52E-02 0.008

Compound: Other PeCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000108 0 0.0000000928 0.000

lb/mmBtuO2 1.07E-12 0.00E+00 9.47E-12 0.000

Sunday, January 30, 2011 Page 21 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

ng/dscm 1.17E-03 0.00E+00 1.05E-02 0.004

ng/dscm@7%O2 1.20E-03 0.00E+00 1.07E-02 0.004

Compound: Other PeCDF

Average

RunNumber 1 2 3

Mass_mg 0 0.0000000996 0.000000134 0.000

lb/mmBtuO2 0.00E+00 1.01E-11 1.37E-11 0.000

ng/dscm 0.00E+00 1.12E-02 1.51E-02 0.009

ng/dscm@7%O2 0.00E+00 1.14E-02 1.54E-02 0.009

Compound: Other TCDD

Average

RunNumber 1 2 3

Mass_mg 0 0 0.0000000393 0.000

lb/mmBtuO2 0.00E+00 0.00E+00 4.01E-12 0.000

ng/dscm 0.00E+00 0.00E+00 4.44E-03 0.001

ng/dscm@7%O2 0.00E+00 0.00E+00 4.54E-03 0.002

Compound: Other TCDF

Average

RunNumber 1 2 3

Mass_mg 0 0 0.0000000618 0.000

lb/mmBtuO2 0.00E+00 0.00E+00 6.31E-12 0.000

ng/dscm 0.00E+00 0.00E+00 6.98E-03 0.002

ng/dscm@7%O2 0.00E+00 0.00E+00 7.13E-03 0.002

Compound: Perylene

Average

RunNumber 1 2 3

Mass_mg 0.00000375 0.00000582 0.0000366 0.000

lb/mmBtuO2 3.71E-10 5.92E-10 3.73E-09 0.000

ng/dscm 4.08E-01 6.55E-01 4.13E+00 1.731

ng/dscm@7%O2 4.20E-01 6.69E-01 4.22E+00 1.770

Compound: Phenanthrene**

Average

RunNumber 1 2 3

Mass_mg 0.00249 0.00212 0.0013 0.002

lb/mmBtuO2 2.46E-07 2.16E-07 1.33E-07 0.000

ng/dscm 2.71E+02 2.39E+02 1.47E+02 219.000

ng/dscm@7%O2 2.79E+02 2.44E+02 1.50E+02 224.333

Compound: Pyrene**

Average

RunNumber 1 2 3

Mass_mg 0.000109 0.000244 0.000407 0.000

lb/mmBtuO2 1.08E-08 2.48E-08 4.15E-08 0.000

ng/dscm 1.18E+01 2.75E+01 4.60E+01 28.433

ng/dscm@7%O2 1.21E+01 2.81E+01 4.70E+01 29.067

Compound: Total Dioxins

Average

RunNumber 1 2 3

Sunday, January 30, 2011 Page 22 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

Mass_mg 0.0000001573 0.0000001708 0.0000003618 0.000

lb/mmBtuO2 1.56E-11 1.74E-11 3.69E-11 0.000

ng/dscm 1.71E-02 1.92E-02 4.09E-02 0.026

ng/dscm@7%O2 1.76E-02 1.96E-02 4.18E-02 0.026

Compound: Total Furans

Average

RunNumber 1 2 3

Mass_mg 0 0.0000003239 0.0000006506 0.000

lb/mmBtuO2 0.00E+00 3.29E-11 6.64E-11 0.000

ng/dscm 0.00E+00 3.65E-02 7.35E-02 0.037

ng/dscm@7%O2 0.00E+00 3.73E-02 7.51E-02 0.037

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 1.86E-03 7.48E-04 7.16E-04 0.001

ppm 3.03E+00 1.25E+00 1.17E+00 1.817

ppm@7%O2 3.14E+00 1.27E+00 1.21E+00 1.873

Location: Stack Exit - Method 25A 3

Compound: Total organic compounds (TOC) as 

Average

Run 4 5 6

lb/mmBtuO2 7.64E-04 9.06E-04 6.20E-04 0.001

ppm 1.25E+00 1.50E+00 1.04E+00 1.263

ppm@7%O2 1.30E+00 1.53E+00 1.06E+00 1.297

Location: Stack Exit - Method 25A 3 6

Compound: Total organic compounds (TOC) as 

Average

Run 7

lb/mmBtuO2 5.10E-04 0.001

ppm 8.58E-01 0.858

ppm@7%O2 8.64E-01 0.864

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 3.1 3.9 3.8 3.600

lb/mmBtuO2 8.02E-04 9.96E-04 9.33E-04 0.001

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.45 0.47 0.48 0.467

lb/mmBtuO2 1.16E-04 1.20E-04 1.18E-04 0.000

Location: Stack Exit - Method 29

Sunday, January 30, 2011 Page 23 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.0064425 0.0287675 0.007405 0.014

lb/mmBtuO2 1.70E-06 5.74E-06 1.47E-06 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.00204 0.001695 0.0011925 0.002

lb/mmBtuO2 5.39E-07 3.38E-07 2.37E-07 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.000415 0.00033 0.000225 0.000

lb/mmBtuO2 1.10E-07 6.58E-08 4.47E-08 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.0002475 0.00012 0.000355 0.000

lb/mmBtuO2 6.54E-08 2.39E-08 7.06E-08 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.00533 0.0064 0.02194 0.011

lb/mmBtuO2 1.41E-06 1.28E-06 4.36E-06 0.000

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.0031025 0.01563 0.003435 0.007

lb/mmBtuO2 8.20E-07 3.12E-06 6.83E-07 0.000

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 1.5 23 22.7 15.733

lb/mmBtuO2 3.96E-04 4.59E-03 4.51E-03 0.003

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.00953 0.01208 0.00621 0.009

lb/mmBtuO2 2.52E-06 2.41E-06 1.23E-06 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.028 0.024275 0.0098 0.021

lb/mmBtuO2 7.40E-06 4.84E-06 1.95E-06 0.000

Sunday, January 30, 2011 Page 24 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.0594 0.2655 0.0677 0.131

lb/mmBtuO2 1.57E-05 5.29E-05 1.35E-05 0.000

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.0086 0.0054875 0.00587 0.007

lb/mmBtuO2 2.27E-06 1.09E-06 1.17E-06 0.000

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

lb/mmBtuO2 2.53E-01 2.47E-01 2.39E-01 0.246

ppm 1.03E+02 1.03E+02 9.77E+01 101.233

ppm@7%O2 1.07E+02 1.05E+02 1.01E+02 104.333

Location: Stack Exit - Method 6C 3

Compound: Sulfur Dioxide

Average

Run 4 5 6

lb/mmBtuO2 2.42E-01 2.43E-01 2.60E-01 0.248

ppm 9.89E+01 1.01E+02 1.09E+02 102.967

ppm@7%O2 1.03E+02 1.03E+02 1.11E+02 105.667

Location: Stack Exit - Method 6C 3 6

Compound: Sulfur Dioxide

Average

Run 7

lb/mmBtuO2 2.58E-01 0.258

ppm 1.09E+02 109.000

ppm@7%O2 1.10E+02 110.000

Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

lb/mmBtuO2 1.59E-01 1.59E-01 1.42E-01 0.153

ppm 9.07E+01 9.29E+01 8.09E+01 88.167

ppm@7%O2 9.41E+01 9.43E+01 8.39E+01 90.767

Location: Stack Exit - Method 7E 3

Compound: Nitrogen oxides (NOx)

Average

Run 4 5 6

lb/mmBtuO2 1.30E-01 1.17E-01 1.13E-01 0.120

ppm 7.38E+01 6.76E+01 6.56E+01 69.000

ppm@7%O2 7.66E+01 6.91E+01 6.66E+01 70.767

Sunday, January 30, 2011 Page 25 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

Process Run Data

Location: Stack Exit - Method 7E 3 6

Compound: Nitrogen oxides (NOx)

Average

Run 7

lb/mmBtuO2 1.14E-01 0.114

ppm 6.68E+01 66.800

ppm@7%O2 6.73E+01 67.300

Location: Stack Exit - OTM - 27/28

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 1.4 6.2 1.6 3.067

lb/mmBtuO2 4.91E-04 2.24E-03 5.65E-04 0.001

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 140 170 180 163.333

lb/mmBtuO2 4.91E-02 6.15E-02 6.36E-02 0.058

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 2.1 2.4 4.5 3.000

lb/mmBtuO2 7.37E-04 8.68E-04 1.59E-03 0.001

Sunday, January 30, 2011 Page 26 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input 668.88 Million Btus/hr Collected during 

M29 run 1

0

10 Heat Input 674.35 Million Btus/hr Collected during 

run 4 of Method 

6C, 7E, 10, and 

25A

0

11 Heat Input 728.64 Million Btus/hr Collected during 

run 5 of Method 

6C, 7E, 10, and 

25A

0

12 Heat Input 689.2 Million Btus/hr Collected during 

run 6 of Method 

6C, 7E, 10, and 

25A

0

13 Heat Input 669.99 Million Btus/hr Collected during 

run 7 of Method 

6C, 7E, 10, and 

25A

0

14 Heat Input 685.18 Million Btus/hr Collected during 

M23 run 1

0

15 Heat Input 705.51 Million Btus/hr Collected during 

M23 run 2

0

16 Heat Input 686.33 Million Btus/hr Collected during 

M23 run 3

0

17 Heat Input 692.11 Million Btus/hr Collected during 

M26A run 1

0

18 Heat Input 742.7 Million Btus/hr Collected during 

M26A run 2

0

19 Heat Input 690.01 Million Btus/hr Collected during 

M26A run 3

0

2 Heat Input 687.78 Million Btus/hr Collected during 

M29 run 2

0

20 Heat Input 681.4 Million Btus/hr Collected during 

M0011 run 1

0

21 Heat Input 661.64 Million Btus/hr Collected during 

M0011 run 2

0

22 Heat Input 636.19 Million Btus/hr Collected during 

M0011 run 3

0

3 Heat Input 671.81 Million Btus/hr Collected during 

M29 run 3

0

4 Heat Input 669.06 Million Btus/hr Collected during 

OTM 27/28 run 1

0

5 Heat Input 687.78 Million Btus/hr Collected during 

OTM 27/28 run 2

0

Sunday, January 30, 2011 Page 27 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

6 Heat Input 668.7 Million Btus/hr Collected during 

OTM 27/28 run 3

0

7 Heat Input 674.1 Million Btus/hr Collected during 

run 1 of Method 

6C, 7E, 10, and 

25A

0

8 Heat Input 669.74 Million Btus/hr Collected during 

run 2 of Method 

6C, 7E, 10, and 

25A

0

9 Heat Input 683.3 Million Btus/hr Collected during 

run 3 of Method 

6C, 7E, 10, and 

25A

0

1 Fuel Oil Firing Rate 55.62 gpm Collected during 

M29 run 1

0

10 Fuel Oil Firing Rate 58.58 gpm Collected during 

run 4 of Method 

6C, 7E, 10, and 

25A

0

11 Fuel Oil Firing Rate 58.58 gpm Collected during 

run 5 of Method 

6C, 7E, 10, and 

25A

0

12 Fuel Oil Firing Rate 58.58 gpm Collected during 

run 6 of Method 

6C, 7E, 10, and 

25A

0

13 Fuel Oil Firing Rate 58.58 gpm Collected during 

run 7 of Method 

6C, 7E, 10, and 

25A

0

14 Fuel Oil Firing Rate 58.58 gpm Collected during 

M23 run 1

0

15 Fuel Oil Firing Rate 58.58 gpm Collected during 

M23 run 2

0

16 Fuel Oil Firing Rate 58.58 gpm Collected during 

M23 run 3

0

17 Fuel Oil Firing Rate 58.58 gpm Collected during 

M26A run 1

0

18 Fuel Oil Firing Rate 58.58 gpm Collected during 

M26A run 2

0

19 Fuel Oil Firing Rate 58.58 gpm Collected during 

M26A run 3

0

2 Fuel Oil Firing Rate 55.62 gpm Collected during 

M29 run 2

0

20 Fuel Oil Firing Rate 58.58 gpm Collected during 

M0011 run 1

0

Sunday, January 30, 2011 Page 28 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

21 Fuel Oil Firing Rate 58.58 gpm Collected during 

M0011 run 2

0

22 Fuel Oil Firing Rate 58.58 gpm Collected during 

M0011 run 3

0

3 Fuel Oil Firing Rate 58.58 gpm Collected during 

M29 run 3

0

4 Fuel Oil Firing Rate 55.62 gpm Collected during 

OTM 27/28 run 1

0

5 Fuel Oil Firing Rate 55.62 gpm Collected during 

OTM 27/28 run 2

0

6 Fuel Oil Firing Rate 58.58 gpm Collected during 

OTM 27/28 run 3

0

7 Fuel Oil Firing Rate 55.62 gpm Collected during 

run 1 of Method 

6C, 7E, 10, and 

25A

0

8 Fuel Oil Firing Rate 55.62 gpm Collected during 

run 2 of Method 

6C, 7E, 10, and 

25A

0

9 Fuel Oil Firing Rate 58.58 gpm Collected during 

run 3 of Method 

6C, 7E, 10, and 

25A

0

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

M29 run 1

0

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

run 4 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

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

run 6 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

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

M23 run 1

0

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

M23 run 2

0

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

M23 run 3

0

Sunday, January 30, 2011 Page 29 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

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

M26A run 1

0

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

M26A run 2

0

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

M26A run 3

0

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

M29 run 2

0

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

M0011 run 1

0

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

M0011 run 2

0

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

M0011 run 3

0

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

M29 run 3

0

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

OTM 27/28 run 1

0

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

OTM 27/28 run 2

0

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

OTM 27/28 run 3

0

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

run 1 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

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

run 3 of Method 

6C, 7E, 10, and 

25A

0

1 Unit Gross Electrical Output 45.41 MW Collected during 

M29 run 1

0

10 Unit Gross Electrical Output 46.86 MW Collected during 

run 4 of Method 

6C, 7E, 10, and 

25A

0

11 Unit Gross Electrical Output 48.33 MW Collected during 

run 5 of Method 

6C, 7E, 10, and 

25A

0

12 Unit Gross Electrical Output 50.21 MW Collected during 

run 6 of Method 

6C, 7E, 10, and 

25A

0

Sunday, January 30, 2011 Page 30 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

13 Unit Gross Electrical Output 49.72 MW Collected during 

run 7 of Method 

6C, 7E, 10, and 

25A

0

14 Unit Gross Electrical Output 46.04 MW Collected during 

M23 run 1

0

15 Unit Gross Electrical Output 47.29 MW Collected during 

M23 run 2

0

16 Unit Gross Electrical Output 50.18 MW Collected during 

M23 run 3

0

17 Unit Gross Electrical Output 48.3 MW Collected during 

M26A run 1

0

18 Unit Gross Electrical Output 49.08 MW Collected during 

M26A run 2

0

19 Unit Gross Electrical Output 50.26 MW Collected during 

M26A run 3

0

2 Unit Gross Electrical Output 46.59 MW Collected during 

M29 run 2

0

20 Unit Gross Electrical Output 50.18 MW Collected during 

M0011 run 1

0

21 Unit Gross Electrical Output 49.19 MW Collected during 

M0011 run 2

0

22 Unit Gross Electrical Output 47.78 MW Collected during 

M0011 run 3

0

3 Unit Gross Electrical Output 46.22 MW Collected during 

M29 run 3

0

4 Unit Gross Electrical Output 45.32 MW Collected during 

OTM 27/28 run 1

0

5 Unit Gross Electrical Output 46.59 MW Collected during 

OTM 27/28 run 2

0

6 Unit Gross Electrical Output 46.2 MW Collected during 

OTM 27/28 run 3

0

7 Unit Gross Electrical Output 46.46 MW Collected during 

run 1 of Method 

6C, 7E, 10, and 

25A

0

8 Unit Gross Electrical Output 44.86 MW Collected during 

run 2 of Method 

6C, 7E, 10, and 

25A

0

9 Unit Gross Electrical Output 46.06 MW Collected during 

run 3 of Method 

6C, 7E, 10, and 

25A

0

1 Unit Net Electric Generation 42.41 MW Collected during 

M29 run 1

0

Sunday, January 30, 2011 Page 31 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

10 Unit Net Electric Generation 43.86 MW Collected during 

run 4 of Method 

6C, 7E, 10, and 

25A

0

11 Unit Net Electric Generation 45.33 MW Collected during 

run 5 of Method 

6C, 7E, 10, and 

25A

0

12 Unit Net Electric Generation 47.21 MW Collected during 

run 6 of Method 

6C, 7E, 10, and 

25A

0

13 Unit Net Electric Generation 46.72 MW Collected during 

run 7 of Method 

6C, 7E, 10, and 

25A

0

14 Unit Net Electric Generation 43.04 MW Collected during 

M23 run 1

0

15 Unit Net Electric Generation 44.29 MW Collected during 

M23 run 2

0

16 Unit Net Electric Generation 47.18 MW Collected during 

M23 run 3

0

17 Unit Net Electric Generation 45.3 MW Collected during 

M26A run 1

0

18 Unit Net Electric Generation 46.08 MW Collected during 

M26A run 2

0

19 Unit Net Electric Generation 47.26 MW Collected during 

M26A run 3

0

2 Unit Net Electric Generation 43.59 MW Collected during 

M29 run 2

0

20 Unit Net Electric Generation 47.18 MW Collected during 

M0011 run 1

0

21 Unit Net Electric Generation 46.19 MW Collected during 

M0011 run 2

0

22 Unit Net Electric Generation 44.78 MW Collected during 

M0011 run 3

0

3 Unit Net Electric Generation 43.22 MW Collected during 

M29 run 3

0

4 Unit Net Electric Generation 42.32 MW Collected during 

OTM 27/28 run 1

0

5 Unit Net Electric Generation 43.59 MW Collected during 

OTM 27/28 run 2

0

6 Unit Net Electric Generation 43.2 MW Collected during 

OTM 27/28 run 3

0

7 Unit Net Electric Generation 43.46 MW Collected during 

run 1 of Method 

6C, 7E, 10, and 

25A

0

Sunday, January 30, 2011 Page 32 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

8 Unit Net Electric Generation 41.86 MW Collected during 

run 2 of Method 

6C, 7E, 10, and 

25A

0

9 Unit Net Electric Generation 43.06 MW Collected during 

run 3 of Method 

6C, 7E, 10, and 

25A

0

1 Fuel Oil Firing Rate 27687 lb/hr Collected during 

M29 run 1

0

10 Fuel Oil Firing Rate 28442 lb/hr Collected during 

run 4 of Method 

6C, 7E, 10, and 

25A

0

11 Fuel Oil Firing Rate 29303 lb/hr Collected during 

run 5 of Method 

6C, 7E, 10, and 

25A

0

12 Fuel Oil Firing Rate 30085 lb/hr Collected during 

run 6 of Method 

6C, 7E, 10, and 

25A

0

13 Fuel Oil Firing Rate 29795 lb/hr Collected during 

run 7 of Method 

6C, 7E, 10, and 

25A

0

14 Fuel Oil Firing Rate 27931 lb/hr Collected during 

M23 run 1

0

15 Fuel Oil Firing Rate 28769 lb/hr Collected during 

M23 run 2

0

16 Fuel Oil Firing Rate 30057 lb/hr Collected during 

M23 run 3

0

17 Fuel Oil Firing Rate 29511 lb/hr Collected during 

M26A run 1

0

18 Fuel Oil Firing Rate 29619 lb/hr Collected during 

M26A run 2

0

19 Fuel Oil Firing Rate 30157 lb/hr Collected during 

M26A run 3

0

2 Fuel Oil Firing Rate 28103 lb/hr Collected during 

M29 run 2

0

20 Fuel Oil Firing Rate 29919 lb/hr Collected during 

M0011 run 1

0

21 Fuel Oil Firing Rate 29632 lb/hr Collected during 

M0011 run 2

0

22 Fuel Oil Firing Rate 29173 lb/hr Collected during 

M0011 run 3

0

3 Fuel Oil Firing Rate 28112 lb/hr Collected during 

M29 run 3

0

Sunday, January 30, 2011 Page 33 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

APCD Run Data

Process Lab Run Data

4 Fuel Oil Firing Rate 27676 lb/hr Collected during 

OTM 27/28 run 1

0

5 Fuel Oil Firing Rate 28103 lb/hr Collected during 

OTM 27/28 run 2

0

6 Fuel Oil Firing Rate 28079 lb/hr Collected during 

OTM 27/28 run 3

0

7 Fuel Oil Firing Rate 28306 lb/hr Collected during 

run 1 of Method 

6C, 7E, 10, and 

25A

0

8 Fuel Oil Firing Rate 27539 lb/hr Collected during 

run 2 of Method 

6C, 7E, 10, and 

25A

0

9 Fuel Oil Firing Rate 28039 lb/hr Collected during 

run 3 of Method 

6C, 7E, 10, and 

25A

0

Run Name Value UOM Comments

Target

Value

1 OVERFIRE AIR 0

1 SELECTIVE NONCATALYTIC REDUCTION 

FOR NOX

0 0

1 ELECTROSTATIC PRECIPITATOR 0 0

Sunday, January 30, 2011 Page 34 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

Sampling / Stack Data Results Detail

Location Stack Exit - Method 0011

Average

Run Number 1 2 3

Test Date 2/25/2010 2/25/2010 2/25/2010

Run Start Time

Run Finish Time

Net Traversing Points 20 20 20

Net Run Time, minutes 120 120 120

Nozzle Diameter, inches 0.374 0.374 0.374 0.374

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.99 0.99 0.99 0.990

Barometric Pressure, inches of Mercury 29.85 29.85 29.85 29.850

Average Orifice Meter Differential, inches H2O 1.61 1.54 1.53 1.560

Dry Gas Meter Volume Sampled, cubic feet 87.262 85.470 84.300 85.677

Average Dry Gas Meter Temperature, °F 79.65 81.35 81.70 80.900

Dry Gas Meter Volume Sampled, dscf 84.661 82.648 81.462 82.924

Total Moisture Liquid collected, g 226 218 232 225.333

Volume of Water Vapor, standard cubic feet 10.64 10.26 10.92 10.607

Moisture Content of Stack Gas, % 11.16 11.04 11.82 11.340

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

Dry Mole Fraction 0.8884 0.8896 0.8818 0.887

Carbon Dioxide, % 10.4 10.4 10.4 10.400

Oxygen, % 7.3 7.3 7.3 7.300

Carbon Monoxide & Nitrogen, % 82.3 82.3 82.3 82.300

Fuel Factor 1.31 1.31 1.31

Dry Molecular Weight, lb/lb-Mole 29.96 29.96 29.96 29.960

Wet Molecular weight, lb/lb-Mole 28.63 28.64 28.55 28.607

Flue Gas Static Pressure, inches of H2O -0.11 -0.05 -0.05 -0.070

Absolute Flue Gas Pressure, inches of Mercury 29.84 29.85 29.85 29.847

Average Stack Gas Temperature, °F 266.75 267.55 269.10 267.800

Average Velocity Head, inches of H2O 0.1204486571

55337

0.114654427

190549

0.114376789

952939

0.116

Average Stack Gas Velocity, feet/second 22.99 22.43 22.46 22.627

Stack Cross-Sectional Area, square feet 173.976 173.976 173.976 173.976

Dry Volumetric Flow Rate, dry scfm 154,480.7 150,805.9 149,365.4 151,550.667

Actual Wet Volumetric Flue Gas Flow Rate, acfm 239,982.5 234,136.9 234,450.1 236,189.833

Percent Isokinetic of Sampling Rate, % 104.1 104.1 103.6 103.933

Percent Excess Air, % 50.6 50.6 50.6 50.600

F-Factor, dscfm/MMBtu @ %O2 9420 9420 9420 9,420.000

Round Duct Diameter, inches 178.6 178.6 178.6

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

Sunday, January 30, 2011 Page 35 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

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

Sunday, January 30, 2011 Page 36 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

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

Sunday, January 30, 2011 Page 37 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

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

Sunday, January 30, 2011 Page 38 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

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

Sunday, January 30, 2011 Page 39 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

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

Sunday, January 30, 2011 Page 40 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

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

Sunday, January 30, 2011 Page 41 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

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

Sunday, January 30, 2011 Page 42 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

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

Sunday, January 30, 2011 Page 43 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

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

Sunday, January 30, 2011 Page 44 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

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

Sunday, January 30, 2011 Page 45 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

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

Sunday, January 30, 2011 Page 46 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

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

Sunday, January 30, 2011 Page 47 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

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

Sunday, January 30, 2011 Page 48 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

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

Sunday, January 30, 2011 Page 49 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

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

Sunday, January 30, 2011 Page 50 of 51
Utility Boiler MACT ICR - Middletown Power Station Unit 2

7/26/2010

Location Stack Exit - OTM - 27/28

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Sunday, January 30, 2011 Page 51 of 51