Name: Lois A. Knowlson

Title: Senior Environmental Engineer

Company: PSEG Fossil

Sign Date: 8/13/2010

Name: Anthony Fortunato

Title: Senior Testing Supervisor

Company: PSEG Maplewood Testing Services

Sign Date: 8/13/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Bridgeport Unit 3 EGU ICR MACT

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.

Tuesday, February 22, 2011 Page 1 of 42
Bridgeport Unit 3 EGU ICR MACT

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Facility Information:

568 - Bridgeport Station

One Atlantic Street

Bridgeport CT 06604

Contact: Michael Stagliola

Phone: 203-551-6001

Fax: 203-551-6139

Email: michael.stagliola@pseg.com

Testing Company:

Maplewood Testing Services

200 Boyden Avenue

Maplewood NJ 07040

Contact: Anthony Fortunato

Phone: 973-761-1005

Fax: 201-572-6185

Email: anthony.fortunato2@pseg.com

Air Permit Number:

015-0217-TV

Permitted Source ID/Name:

EMU3 Unit 3

Permitted Maximum Process Rate:

230 tons of coal per hour

Max. Normal Operation Process Rate:

221 tons coal per hour (Jan. 3, 2

Target Process Test Rate

175 tons coal per hour

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

 process flow diagram:

PSEG Power Connecticut, LLC, Bridgeport Harbor Station (ORIS 568), Unit 3 (EMU3) is an electric-generating 

boiler, configured as a tangentially-fired, dry-bottom unit, utilizing sub-bituminous, low-sulfur coal. 

This description should describe the process and associated controls to differentiate this facility from, or document 

similarity with others of same SCC.

Industry/SCC/NAIS 221112

Sampling Location Information:

AFS #: 0900100027, 090010906 FRS #: 110000316989

SCC / Description 10100202 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Pulverized Coal: Dry Bottom (Bituminous Coal) 

The following state and federal regulations that apply to the proposed testing:

Location

Round

Duct

Diam.

Distance from 

upstream dist.

Distance from

downstream dist.

Number of

Traverse Ports

Equiv. 

Diam

Min.Travers 

Points

Rect. Duct 

Length /Width

Stack Exit 18.5 196.7 196.7 18.5 2304 2988 4 24

Regulation Description Compound Limit Unit

RCSA Section 22a-174-18(e)(1) Total Particulate 0.1 lb/million BTU 

using O2

CGS Section 22a-199(b)(1) Mercury 0.0006 lb/million BTU 

using O2

RCSA Section 22a-174-22(d)(2) and (e)(3) - 24 hour 

average

Nitrogen oxides (NOx) 0.38 lb/million BTU 

using O2

RCSA Section 22a-174-22(d)(2) and (e)(3) - 7 month 

average (10/1-4/30)

Nitrogen oxides (NOx) 0.15 lb/million BTU 

using O2

RCSA Section 22a-174-19a(e) - Calendar quarter Sulfur Dioxide 0.33 lb/million BTU 

using O2

Tuesday, February 22, 2011 Page 2 of 42
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Test Parameter Information:

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Exit % H2O Method 1 - 4 3 180 0

Stack Exit Carbon Monoxide Method 10 3 120 0

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

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

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 3 120 0

Stack Exit Hydrogen Fluoride Method 26A 3 180 0

Stack Exit Hydrogen Chloride Method 26A 3 180 0

Stack Exit Hydrogen Fluoride Method 26 3 180 0

Tuesday, February 22, 2011 Page 3 of 42
Bridgeport Unit 3 EGU ICR MACT

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The following describes any modifications and/or deviations to the applicable test 

methods. If alternative methods were requested, see the attachments for documentation 

of request AND approval, including dates.

Not applicable

Stack Exit Hydrogen Chloride Method 26 3 180 0

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Inorganic (Aqueous) 

Condensible Part.

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Organic Condensible 

Particulate

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Stack Exit Beryllium Method 29 3 240 0

Stack Exit Cobalt Method 29 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Antimony Method 29 3 240 0

Stack Exit Arsenic Method 29 3 240 0

Stack Exit Selenium Method 29 3 240 0

Stack Exit Lead Method 29 3 240 0

Stack Exit Filterable Particulate Method 29 3 240 0

Stack Exit Chromium Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Cadmium Method 29 3 240 0

Stack Exit O2 Method 3A O2 3 240 0

Stack Exit O2 Method 3A O2 3 120 0

Stack Exit Co2 Method 3A CO2 3 120 0

Stack Exit Co2 Method 3A CO2 3 240 0

Stack Exit O2 Method 3A O2 3 480 0

Stack Exit Co2 Method 3A CO2 3 480 0

Total Particulate Method 5/OTM-28 3 240 0 Use only for wet 

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Inorganic (Aqueous) 

Condensible Part.

Method 5/OTM-28 3 240 0 Use only for wet 

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Organic Condensible 

Particulate

Method 5/OTM-28 3 240 0 Use only for wet 

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Stack Exit Filterable Particulate Method 5 3 240 0

Filterable Particulate Method 5/OTM-28 3 240 0 Use only for wet 

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Stack Exit Sulfur Dioxide Method 6C 3 180 0

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

Tuesday, February 22, 2011 Page 4 of 42
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Tuesday, February 22, 2011 Page 5 of 42
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Tuesday, February 22, 2011 Page 6 of 42
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Sampling / Stack Data Results Summary

Location Stack Exit - Method 0011

Average

Run Number 1-1 1-2 1-3

Test Date 4/16/2010 4/16/2010 4/16/2010

Run Start Time 11:10:00 AM 2:16:00 PM 5:23:00 PM

Run Finish Time 1:25:00 PM 4:34:00 PM 7:50:00 PM

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 76.662 75.214 74.314 75.397

Moisture Content of Stack Gas, % 12.15 12.27 12.46 12.293

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

Carbon Dioxide, % 15.5 15.3 15.2 15.333

Oxygen, % 4.2 4.3 4.3 4.267

Average Stack Gas Temperature, °F 293.00 293.83 294.08 293.637

Dry Volumetric Flow Rate, dry scfm 856,991.8 837,143.2 828,730.0 840,955.000

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,386,586.1 1,370,142.5 1,361,598.2 1,372,775.60

0

Percent Isokinetic of Sampling Rate, % 98.6 99.0 98.8 98.800

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

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

Tuesday, February 22, 2011 Page 7 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

Location Stack Exit - Method 25A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack Exit - Method 26A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Tuesday, February 22, 2011 Page 8 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

Location Stack Exit - Method 29 

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Location Stack Exit - Method 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

Tuesday, February 22, 2011 Page 9 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

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 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

Tuesday, February 22, 2011 Page 10 of 42
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8/13/2010

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

Tuesday, February 22, 2011 Page 11 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

Emissions Summary

Location: Stack Exit - Method 0011

Compound: Formaldehyde

Average

RunNumber 1-1 1-2 1-3

Mass_mg 0.006 0.01 0.001 0.006

lb/mmBtuO2 2.11E-06 3.61E-06 3.65E-07 0.000

ppm 2.21E-03 3.76E-03 3.81E-04 0.002

ppm@7%O2 1.84E-03 3.15E-03 3.19E-04 0.002

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

Elb/hr 2.61E+02 3.31E+02 3.19E+02 303.667

gr/dscf 3.56E-02 4.40E-02 4.48E-02 0.041

lb/mmBtuO2 6.22E-02 7.75E-02 7.89E-02 0.073

mg/dscm 8.14E+01 1.01E+02 1.03E+02 95.133

ppm 6.99E+01 8.65E+01 8.81E+01 81.500

ppm@7%O2 5.82E+01 7.24E+01 7.38E+01 68.133

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000

gr/dscf 0.00E+00 0.00E+00 0.00E+00 0.000

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

mg/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ppm 0.00E+00 0.00E+00 0.00E+00 0.000

ppm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 3-1 3-2 3-3

Mass_mg 8.2 3.8 3.7 5.233

Elb/hr 8.13E+00 3.70E+00 1.06E+01 7.477

lb/mmBtuO2 2.01E-03 9.01E-04 2.79E-03 0.002

mg/dscm 2.63E+00 1.18E+00 3.65E+00 2.487

mg/dscm@7%O2 2.19E+00 9.82E-01 3.04E+00 2.071

Compound: Hydrogen Fluoride

Average

RunNumber 3-1 3-2 3-3

Mass_mg 0.52 0.51 0.51 0.513

Elb/hr 5.16E-01 4.96E-01 1.46E+00 0.824

lb/mmBtuO2 1.27E-04 1.21E-04 3.84E-04 0.000

mg/dscm 1.67E-01 1.58E-01 5.03E-01 0.276

mg/dscm@7%O2 1.39E-01 1.32E-01 4.19E-01 0.230

Tuesday, February 22, 2011 Page 12 of 42
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Location: Stack Exit - Method 29 

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.00036 0.00036 0.00036 0.000

Elb/hr 2.75E-04 2.83E-04 2.76E-04 0.000

lb/mmBtuO2 6.24E-08 6.75E-08 6.60E-08 0.000

mg/dscm 8.24E-05 8.73E-05 8.51E-05 0.000

mg/dscm@7%O2 6.79E-05 7.35E-05 7.19E-05 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.00308 0.00096 0.00085 0.002

Elb/hr 2.35E-03 7.54E-04 6.51E-04 0.001

lb/mmBtuO2 5.34E-07 1.80E-07 1.56E-07 0.000

mg/dscm 7.05E-04 2.33E-04 2.01E-04 0.000

mg/dscm@7%O2 5.81E-04 1.96E-04 1.70E-04 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.000448 0.00033 0.00033 0.000

Elb/hr 3.42E-04 2.59E-04 2.53E-04 0.000

lb/mmBtuO2 7.76E-08 6.19E-08 6.05E-08 0.000

mg/dscm 1.03E-04 8.00E-05 7.80E-05 0.000

mg/dscm@7%O2 8.49E-05 6.74E-05 6.59E-05 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.00023 0.000234 0.00023 0.000

Elb/hr 1.76E-04 1.84E-04 1.76E-04 0.000

lb/mmBtuO2 3.99E-08 4.39E-08 4.22E-08 0.000

mg/dscm 5.27E-05 5.68E-05 5.44E-05 0.000

mg/dscm@7%O2 4.34E-05 4.78E-05 4.60E-05 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.00504 0.00274 0.00253 0.003

Elb/hr 3.85E-03 2.15E-03 1.94E-03 0.003

lb/mmBtuO2 8.73E-07 5.14E-07 4.64E-07 0.000

mg/dscm 1.15E-03 6.65E-04 5.98E-04 0.001

mg/dscm@7%O2 9.48E-04 5.60E-04 5.05E-04 0.001

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.00265 0.00017 0.00011 0.001

Elb/hr 2.02E-03 1.33E-04 8.43E-05 0.001

lb/mmBtuO2 4.59E-07 3.19E-08 2.02E-08 0.000

mg/dscm 6.07E-04 4.12E-05 2.60E-05 0.000

Tuesday, February 22, 2011 Page 13 of 42
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mg/dscm@7%O2 5.00E-04 3.47E-05 2.20E-05 0.000

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 2.1 2.2 2.4 2.233

Elb/hr 1.60E+00 1.73E+00 1.84E+00 1.723

lb/mmBtuO2 3.64E-04 4.12E-04 4.40E-04 0.000

mg/dscm 4.81E-01 5.34E-01 5.67E-01 0.527

mg/dscm@7%O2 3.97E-01 4.50E-01 4.79E-01 0.442

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.00347 0.0015 0.000872 0.002

Elb/hr 2.65E-03 1.18E-03 6.68E-04 0.001

lb/mmBtuO2 6.01E-07 2.81E-07 1.60E-07 0.000

mg/dscm 7.95E-04 3.64E-04 2.06E-04 0.000

mg/dscm@7%O2 6.55E-04 3.06E-04 1.74E-04 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.0416 0.00392 0.00377 0.016

Elb/hr 3.18E-02 3.08E-03 2.89E-03 0.013

lb/mmBtuO2 7.21E-06 7.35E-07 6.91E-07 0.000

mg/dscm 9.53E-03 9.51E-04 8.91E-04 0.004

mg/dscm@7%O2 7.86E-03 8.01E-04 7.53E-04 0.003

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.00721 0.00469 0.006 0.006

Elb/hr 5.50E-03 3.68E-03 4.60E-03 0.005

lb/mmBtuO2 1.25E-06 8.79E-07 1.10E-06 0.000

mg/dscm 1.65E-03 1.14E-03 1.42E-03 0.001

mg/dscm@7%O2 1.36E-03 9.60E-04 1.20E-03 0.001

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.0039 0.0028 0.0029 0.003

Elb/hr 2.98E-03 2.20E-03 2.22E-03 0.002

lb/mmBtuO2 6.76E-07 5.25E-07 5.32E-07 0.000

mg/dscm 8.93E-04 6.79E-04 6.85E-04 0.001

mg/dscm@7%O2 7.36E-04 5.72E-04 5.79E-04 0.001

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Run 1-1 1-2 1-3

Elb/hr 7.78E+02 7.87E+02 7.46E+02 770.333

lb/mmBtuO2 1.85E-01 1.84E-01 1.85E-01 0.185

Tuesday, February 22, 2011 Page 14 of 42
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mg/dscm 2.42E+02 2.40E+02 2.40E+02 240.667

mg/dscm@7%O2 2.01E+02 2.01E+02 2.01E+02 201.000

ppm 9.10E+01 8.99E+01 9.02E+01 90.367

ppm@7%O2 7.57E+01 7.53E+01 7.55E+01 75.500

Location: Stack Exit - Method 6C 3

Compound: Sulfur Dioxide

Average

Run 3-1 3-2 3-3

Elb/hr 7.08E+02 6.96E+02 7.07E+02 703.667

lb/mmBtuO2 1.73E-01 1.71E-01 1.86E-01 0.177

mg/dscm 2.26E+02 2.24E+02 2.44E+02 231.333

mg/dscm@7%O2 1.88E+02 1.86E+02 2.03E+02 192.333

ppm 8.48E+01 8.42E+01 9.15E+01 86.833

ppm@7%O2 7.06E+01 7.01E+01 7.62E+01 72.300

Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 3-1 3-2 3-3

Elb/hr 5.28E+02 5.14E+02 4.94E+02 512.000

lb/mmBtuO2 1.28E-01 1.28E-01 1.32E-01 0.129

mg/dscm 1.69E+02 1.65E+02 1.71E+02 168.333

mg/dscm@7%O2 1.39E+02 1.39E+02 1.44E+02 140.667

ppm 8.82E+01 8.65E+01 8.92E+01 87.967

ppm@7%O2 7.27E+01 7.28E+01 7.54E+01 73.633

Location: Stack Exit - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 4-1 4-2 4-3

Mass_mg 4.9 5.5 6 5.467

Elb/hr 5.37E+00 4.72E+00 5.16E+00 5.083

Elb/min 8.95E-02 7.87E-02 8.60E-02 0.085

gr/dscf 7.17E-04 6.35E-04 6.83E-04 0.001

lb/mmBtuO2 1.24E-03 1.12E-03 1.21E-03 0.001

mg/dscm 1.64E+00 1.45E+00 1.56E+00 1.550

Compound: Filterable PM2.5

Average

RunNumber 4-1 4-2 4-3

Mass_mg 4.4 5 5.5 4.967

Elb/hr 4.82E+00 4.29E+00 4.73E+00 4.613

Elb/min 8.03E-02 7.16E-02 7.88E-02 0.077

gr/dscf 6.44E-04 5.77E-04 6.26E-04 0.001

lb/mmBtuO2 1.12E-03 1.02E-03 1.11E-03 0.001

mg/dscm 1.47E+00 1.32E+00 1.43E+00 1.407

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 4-1 4-2 4-3

Mass_mg 4.8 25 4.4 11.400

Tuesday, February 22, 2011 Page 15 of 42
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Process Run Data

Elb/hr 5.26E+00 2.15E+01 3.78E+00 10.180

Elb/min 8.77E-02 3.58E-01 6.31E-02 0.170

gr/dscf 7.03E-04 2.89E-03 5.01E-04 0.001

lb/mmBtuO2 1.22E-03 5.10E-03 8.89E-04 0.002

mg/dscm 1.61E+00 6.61E+00 1.15E+00 3.123

Compound: Organic Condensible Particulate

Average

RunNumber 4-1 4-2 4-3

Mass_mg 2.8 2.2 1.5 2.167

Elb/hr 3.07E+00 1.89E+00 1.29E+00 2.083

Elb/min 5.11E-02 3.15E-02 2.15E-02 0.035

gr/dscf 4.10E-04 2.54E-04 1.71E-04 0.000

lb/mmBtuO2 7.10E-04 4.49E-04 3.03E-04 0.000

mg/dscm 9.38E-01 5.81E-01 3.91E-01 0.637

Compound: Total Particulate

Average

RunNumber 4-1 4-2 4-3

Mass_mg 12.5 32.7 11.9 19.033

Elb/hr 1.37E+01 2.81E+01 1.02E+01 17.333

Elb/min 2.28E-01 4.68E-01 1.71E-01 0.289

gr/dscf 1.83E-03 3.78E-03 1.35E-03 0.002

lb/mmBtuO2 3.17E-03 6.68E-03 2.40E-03 0.004

mg/dscm 4.19E+00 8.64E+00 3.10E+00 5.310

Compound: Total PM2.5

Average

RunNumber 4-1 4-2 4-3

Mass_mg 12 32.2 11.4 18.533

Elb/hr 1.31E+01 2.76E+01 9.80E+00 16.833

Elb/min 2.19E-01 4.61E-01 1.63E-01 0.281

gr/dscf 1.76E-03 3.72E-03 1.30E-03 0.002

lb/mmBtuO2 3.04E-03 6.57E-03 2.30E-03 0.004

mg/dscm 4.02E+00 8.51E+00 2.97E+00 5.167

Tuesday, February 22, 2011 Page 16 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

2 Unit Gross Electrical Output 398 Mwe BHS3 Group 1 

Runs 1-4 M0031 

Start 4/16/2010 

11:20 End 

4/16/2010 13:21

0

2 Unit Net Electric Generation 382 MWh BHS3 Group 1 

Runs 1-4 M0031 

Start 4/16/2010 

11:20 End 

4/16/2010 13:21

0

3 Unit Gross Electrical Output 398 Mwe BHS3 Group 1 

Run 1 M18 (CH4) 

Start 4/16/2010 

18:10 End 

4/16/2010 18:12

0

3 Unit Net Electric Generation 382 MWh BHS3 Group 1 

Run 1 M18 (CH4) 

Start 4/16/2010 

18:10 End 

4/16/2010 18:12

0

1 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 1 

Run 1M0010 Start 

4/16/2010 11:10 

End 4/16/2010 

13:25

0

2 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 1 

Runs 1-4 M0031 

Start 4/16/2010 

11:20 End 

4/16/2010 13:21

0

3 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 1 

Run 1 M18 (CH4) 

Start 4/16/2010 

18:10 End 

4/16/2010 18:12

0

4 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 1 

Run 1 M6C (SO2) 

Start 4/16/2010 

11:10 End 

4/16/2010 13:09

0

5 Sorbent Injection Rate 35.3 lb/hr BHS3 Group 1 

Run 1 M10 (CO) 

Start 4/16/2010 

11:10 End 

4/16/2010 

13:092010 13:09

0

Tuesday, February 22, 2011 Page 17 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

6 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 1 

Run 1 M25A 

(TOC as propane) 

Start 4/16/2010 

11:10 End 

4/16/2010 13:09

0

7 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 1 

Run 2 M0010 

Start 4/16/2010 

14:16 End 

4/16/2010 16:34

0

8 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 1 

Run 2 M0011 

Start 4/16/2010 

14:16 End 

4/16/2010 16:34

0

9 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 1 

Runs 5-8 M0031 

Start 4/16/2010 

14:23 End 

4/16/2010 16:32

0

10 Coal Burned 0.212 1000 Tons/hr BHS3 Group 1 

Run 1M0011 Start 

4/16/2010 11:10 

End 4/16/2010 

13:25

0

10 Unit Gross Electrical Output 398 Mwe BHS3 Group 1 

Run 1M0011 Start 

4/16/2010 11:10 

End 4/16/2010 

13:25

0

10 Unit Net Electric Generation 382 MWh BHS3 Group 1 

Run 1M0011 Start 

4/16/2010 11:10 

End 4/16/2010 

13:25

0

10 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 1 

Run 1M0011 Start 

4/16/2010 11:10 

End 4/16/2010 

13:25

0

11 Coal Burned 0.21 1000 Tons/hr BHS3 Group 1 

Run 2 M18 (CH4) 

Start 4/16/2010 

18:20 End 

4/16/2010 18:24

0

11 Unit Gross Electrical Output 35.5 Mwe BHS3 Group 1 

Run 2 M18 (CH4) 

Start 4/16/2010 

18:20 End 

4/16/2010 18:24

0

Tuesday, February 22, 2011 Page 18 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

11 Unit Net Electric Generation 398 MWh BHS3 Group 1 

Run 2 M18 (CH4) 

Start 4/16/2010 

18:20 End 

4/16/2010 18:24

0

11 Sorbent Injection Rate 383 lb/hr BHS3 Group 1 

Run 2 M18 (CH4) 

Start 4/16/2010 

18:20 End 

4/16/2010 18:24

0

12 Coal Burned 0.211 1000 Tons/hr BHS3 Group 1 

Run 2 M6C (SO2) 

Start 4/16/2010 

14:35 End 

4/16/2010 16:34

0

12 Unit Gross Electrical Output 398 Mwe BHS3 Group 1 

Run 2 M6C (SO2) 

Start 4/16/2010 

14:35 End 

4/16/2010 16:34

0

12 Unit Net Electric Generation 383 MWh BHS3 Group 1 

Run 2 M6C (SO2) 

Start 4/16/2010 

14:35 End 

4/16/2010 16:34

0

12 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 1 

Run 2 M6C (SO2) 

Start 4/16/2010 

14:35 End 

4/16/2010 16:34

0

13 Coal Burned 0.211 1000 Tons/hr BHS3 Group 1 

Run 2 M10 (CO) 

Start 4/16/2010 

14:35 End 

4/16/2010 16:34

0

13 Unit Gross Electrical Output 398 Mwe BHS3 Group 1 

Run 2 M10 (CO) 

Start 4/16/2010 

14:35 End 

4/16/2010 16:34

0

13 Unit Net Electric Generation 383 MWh BHS3 Group 1 

Run 2 M10 (CO) 

Start 4/16/2010 

14:35 End 

4/16/2010 16:34

0

Tuesday, February 22, 2011 Page 19 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

13 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 1 

Run 2 M10 (CO) 

Start 4/16/2010 

14:35 End 

4/16/2010 

16:34End 

4/16/2010	16:34

0

14 Coal Burned 0.211 1000 Tons/hr BHS3 Group 1 

Run 2 M25A 

(TOC as propane) 

Start 4/16/2010 

14:35 End 

4/16/2010 16:34

0

14 Unit Gross Electrical Output 398 Mwe BHS3 Group 1 

Run 2 M25A 

(TOC as propane) 

Start 4/16/2010 

14:35 End 

4/16/2010 16:34

0

14 Unit Net Electric Generation 383 MWh BHS3 Group 1 

Run 2 M25A 

(TOC as propane) 

Start 4/16/2010 

14:35 End 

4/16/2010 16:34

0

14 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 1 

Run 2 M25A 

(TOC as propane) 

Start 4/16/2010 

14:35 End 

4/16/2010 16:34

0

15 Coal Burned 0.212 1000 Tons/hr BHS3 Group 1 

Run 3 M0010 

Start 4/16/2010 

17:23 End 

4/16/2010 19:50

0

15 Unit Gross Electrical Output 398 Mwe BHS3 Group 1 

Run 3 M0010 

Start 4/16/2010 

17:23 End 

4/16/2010 19:50

0

15 Unit Net Electric Generation 382 MWh BHS3 Group 1 

Run 3 M0010 

Start 4/16/2010 

17:23 End 

4/16/2010 19:50

0

15 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 1 

Run 3 M0010 

Start 4/16/2010 

17:23 End 

4/16/2010 19:50

0

Tuesday, February 22, 2011 Page 20 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

16 Coal Burned 0.212 1000 Tons/hr BHS3 Group 1 

Run 3 M0011 

Start 4/16/2010 

17:23 End 

4/16/2010 19:50

0

16 Unit Gross Electrical Output 398 Mwe BHS3 Group 1 

Run 3 M0011 

Start 4/16/2010 

17:23 End 

4/16/2010 19:50

0

16 Unit Net Electric Generation 382 MWh BHS3 Group 1 

Run 3 M0011 

Start 4/16/2010 

17:23 End 

4/16/2010 19:50

0

16 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 1 

Run 3 M0011 

Start 4/16/2010 

17:23 End 

4/16/2010 19:50

0

17 Coal Burned 0.212 1000 Tons/hr BHS3 Group 1 

Runs 9-12 M0031 

Start 4/16/2010 

17:28 End 

4/16/2010 19:32

0

17 Unit Gross Electrical Output 398 Mwe BHS3 Group 1 

Runs 9-12 M0031 

Start 4/16/2010 

17:28 End 

4/16/2010 19:32

0

17 Unit Net Electric Generation 382 MWh BHS3 Group 1 

Runs 9-12 M0031 

Start 4/16/2010 

17:28 End 

4/16/2010 19:32

0

17 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 1 

Runs 9-12 M0031 

Start 4/16/2010 

17:28 End 

4/16/2010 19:32

0

18 Coal Burned 0.212 1000 Tons/hr BHS3 Group 1 

Run 3 M18 

(CH4)	Start 

4/16/2010 20:00 

End 4/16/2010 

20:03

0

Tuesday, February 22, 2011 Page 21 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

18 Unit Gross Electrical Output 398 Mwe BHS3 Group 1 

Run 3 M18 

(CH4)	Start 

4/16/2010 20:00 

End 4/16/2010 

20:0320:03

0

18 Unit Net Electric Generation 382 MWh BHS3 Group 1 

Run 3 M18 

(CH4)	Start 

4/16/2010 20:00 

End 4/16/2010 

20:03

0

18 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 1 

Run 3 M18 

(CH4)	Start 

4/16/2010 20:00 

End 4/16/2010 

20:03

0

19 Coal Burned 0.212 1000 Tons/hr BHS3 Group 1 

Run 3 M6C (SO2) 

Start 4/16/2010 

17:23 End 

4/16/2010 19:22

0

19 Unit Gross Electrical Output 398 Mwe BHS3 Group 1 

Run 3 M6C (SO2) 

Start 4/16/2010 

17:23 End 

4/16/2010 19:22

0

19 Unit Net Electric Generation 382 MWh BHS3 Group 1 

Run 3 M6C (SO2) 

Start 4/16/2010 

17:23 End 

4/16/2010 19:22

0

19 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 1 

Run 3 M6C (SO2) 

Start 4/16/2010 

17:23 End 

4/16/2010 19:22

0

20 Coal Burned 0.212 1000 Tons/hr BHS3 Group 1 

Run 3 M10 (CO) 

Start 4/16/2010 

17:23 End 

4/16/2010 19:22

0

20 Unit Gross Electrical Output 398 Mwe BHS3 Group 1 

Run 3 M10 (CO) 

Start 4/16/2010 

17:23 End 

4/16/2010 19:22

0

Tuesday, February 22, 2011 Page 22 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

20 Unit Net Electric Generation 382 MWh BHS3 Group 1 

Run 3 M10 (CO) 

Start 4/16/2010 

17:23 End 

4/16/2010 19:22

0

20 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 1 

Run 3 M10 (CO) 

Start 4/16/2010 

17:23 End 

4/16/2010 19:22

0

21 Coal Burned 0.212 1000 Tons/hr BHS3 Group 1 

Run 3 M25A 

(TOC as propane) 

Start 4/16/2010 

17:23 End 

4/16/2010 19:22

0

21 Unit Gross Electrical Output 398 Mwe BHS3 Group 1 

Run 3 M25A 

(TOC as propane) 

Start 4/16/2010 

17:23 End 

4/16/2010 19:22

0

21 Unit Net Electric Generation 382 MWh BHS3 Group 1 

Run 3 M25A 

(TOC as propane) 

Start 4/16/2010 

17:23 End 

4/16/2010 19:22

0

21 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 1 

Run 3 M25A 

(TOC as propane) 

Start 4/16/2010 

17:23 End 

4/16/2010 19:22

0

22 Coal Burned 0.217 1000 Tons/hr BHS3 Group 3 

Run 1 M26A End 

4/13/2010 12:10 

End 4/13/2010 

15:40

0

22 Unit Gross Electrical Output 401 Mwe BHS3 Group 3 

Run 1 M26A End 

4/13/2010 12:10 

End 4/13/2010 

15:40

0

22 Unit Net Electric Generation 385 MWh BHS3 Group 3 

Run 1 M26A End 

4/13/2010 12:10 

End 4/13/2010 

15:40

0

Tuesday, February 22, 2011 Page 23 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

22 Sorbent Injection Rate 35.6 lb/hr BHS3 Group 3 

Run 1 M26A End 

4/13/2010 12:10 

End 4/13/2010 

15:40

0

23 Coal Burned 0.217 1000 Tons/hr BHS3 Group 3 

Run 1 M6C (SO2) 

End 4/13/2010 

12:10 End 

4/13/2010 14:09

0

23 Unit Gross Electrical Output 401 Mwe BHS3 Group 3 

Run 1 M6C (SO2) 

End 4/13/2010 

12:10 End 

4/13/2010 14:09

0

23 Unit Net Electric Generation 385 MWh BHS3 Group 3 

Run 1 M6C (SO2) 

End 4/13/2010 

12:10 End 

4/13/2010 14:09

0

23 Sorbent Injection Rate 35.6 lb/hr BHS3 Group 3 

Run 1 M6C (SO2) 

End 4/13/2010 

12:10 End 

4/13/2010 14:09

0

24 Coal Burned 0.217 1000 Tons/hr BHS3 Group 3 

Run 1 M7E (NOx) 

End 4/13/2010 

12:10 End 

4/13/2010 14:09

0

24 Unit Gross Electrical Output 401 Mwe BHS3 Group 3 

Run 1 M7E (NOx) 

End 4/13/2010 

12:10 End 

4/13/2010 14:09

0

24 Unit Net Electric Generation 385 MWh BHS3 Group 3 

Run 1 M7E (NOx) 

End 4/13/2010 

12:10 End 

4/13/2010 14:09

0

24 Sorbent Injection Rate 35.6 lb/hr BHS3 Group 3 

Run 1 M7E (NOx) 

End 4/13/2010 

12:10 End 

4/13/2010 14:09

0

25 Coal Burned 0.216 1000 Tons/hr BHS3 Group 3 

Run 2 M26A Start 

4/13/2010 16:36 

End 4/13/2010 

20:17

0

Tuesday, February 22, 2011 Page 24 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

25 Unit Gross Electrical Output 402 Mwe BHS3 Group 3 

Run 2 M26A Start 

4/13/2010 16:36 

End 4/13/2010 

20:17

0

25 Unit Net Electric Generation 386 MWh BHS3 Group 3 

Run 2 M26A Start 

4/13/2010 16:36 

End 4/13/2010 

20:17	20:17

0

25 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 3 

Run 2 M26A Start 

4/13/2010 16:36 

End 4/13/2010 

20:17

0

26 Coal Burned 0.216 1000 Tons/hr BHS3 Group 3 

Run 2 M6C (SO2) 

Start 4/13/2010 

16:35 End 

4/13/2010 18:34

0

26 Unit Gross Electrical Output 402 Mwe BHS3 Group 3 

Run 2 M6C (SO2) 

Start 4/13/2010 

16:35 End 

4/13/2010 18:34

0

26 Unit Net Electric Generation 386 MWh BHS3 Group 3 

Run 2 M6C (SO2) 

Start 4/13/2010 

16:35 End 

4/13/2010 18:34

0

26 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 3 

Run 2 M6C (SO2) 

Start 4/13/2010 

16:35 End 

4/13/2010 18:34

0

27 Coal Burned 0.216 1000 Tons/hr BHS3 Group 3 

Run 2 M7E (NOx) 

Start 4/13/2010 

16:35 End 

4/13/2010 18:34

0

27 Unit Gross Electrical Output 402 Mwe BHS3 Group 3 

Run 2 M7E (NOx) 

Start 4/13/2010 

16:35 End 

4/13/2010 18:34

0

27 Unit Net Electric Generation 386 MWh BHS3 Group 3 

Run 2 M7E (NOx) 

Start 4/13/2010 

16:35 End 

4/13/2010 18:34

0

Tuesday, February 22, 2011 Page 25 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

27 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 3 

Run 2 M7E (NOx) 

Start 4/13/2010 

16:35 End 

4/13/2010 18:34

0

28 Coal Burned 0.212 1000 Tons/hr BHS3 Group 3 

Run 3 M26A Start 

4/16/2010 20:31 

End 4/16/2010 

21:41

0

28 Unit Gross Electrical Output 398 Mwe BHS3 Group 3 

Run 3 M26A Start 

4/16/2010 20:31 

End 4/16/2010 

21:41

0

28 Unit Net Electric Generation 382 MWh BHS3 Group 3 

Run 3 M26A Start 

4/16/2010 20:31 

End 4/16/2010 

21:41

0

28 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 3 

Run 3 M26A Start 

4/16/2010 20:31 

End 4/16/2010 

21:41

0

29 Coal Burned 0.212 1000 Tons/hr BHS3 Group 3 

Run 3 M6C (SO2) 

Start 4/16/2010 

20:31 End 

4/16/2010 21:30

0

29 Unit Gross Electrical Output 398 Mwe BHS3 Group 3 

Run 3 M6C (SO2) 

Start 4/16/2010 

20:31 End 

4/16/2010 21:30

0

29 Unit Net Electric Generation 382 MWh BHS3 Group 3 

Run 3 M6C (SO2) 

Start 4/16/2010 

20:31 End 

4/16/2010 21:30

0

29 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 3 

Run 3 M6C (SO2) 

Start 4/16/2010 

20:31 End 

4/16/2010 21:30

0

30 Coal Burned 0.212 1000 Tons/hr BHS3 Group 3 

Run 3 M7E (NOx) 

Start 4/16/2010 

20:31 End 

4/16/2010 21:30

0

Tuesday, February 22, 2011 Page 26 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

30 Unit Gross Electrical Output 398 Mwe BHS3 Group 3 

Run 3 M7E (NOx) 

Start 4/16/2010 

20:31 End 

4/16/2010 21:30

0

30 Unit Net Electric Generation 382 MWh BHS3 Group 3 

Run 3 M7E (NOx) 

Start 4/16/2010 

20:31 End 

4/16/2010 21:30

0

30 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 3 

Run 3 M7E (NOx) 

Start 4/16/2010 

20:31 End 

4/16/2010 21:30

0

31 Coal Burned 0.214 1000 Tons/hr BHS3 Group 4 

Run 1 M29 Start 

4/14/2010 15:45 

End 4/14/2010 

20:02

0

31 Unit Gross Electrical Output 398 Mwe BHS3 Group 4 

Run 1 M29 Start 

4/14/2010 15:45 

End 4/14/2010 

20:02

0

31 Unit Net Electric Generation 383 MWh BHS3 Group 4 

Run 1 M29 Start 

4/14/2010 15:45 

End 4/14/2010 

20:02

0

31 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 4 

Run 1 M29 Start 

4/14/2010 15:45 

End 4/14/2010 

20:02

0

32 Coal Burned 0.214 1000 Tons/hr BHS3 Group 4 

Run 1 

OTM027/028 Start 

4/14/2010 15:45 

End 4/14/2010 

21:43

0

32 Unit Gross Electrical Output 399 Mwe BHS3 Group 4 

Run 1 

OTM027/028 Start 

4/14/2010 15:45 

End 4/14/2010 

21:43

0

Tuesday, February 22, 2011 Page 27 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

32 Unit Net Electric Generation 384 MWh BHS3 Group 4 

Run 1 

OTM027/028 Start 

4/14/2010 15:45 

End 4/14/2010 

21:43

0

32 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 4 

Run 1 

OTM027/028 Start 

4/14/2010 15:45 

End 4/14/2010 

21:43

0

33 Coal Burned 0.21 1000 Tons/hr BHS3 Group 4 

Run 1 M30B Start 

4/15/2010 8:57 

End 4/14/2010 

10:57

0

33 Unit Gross Electrical Output 391 Mwe BHS3 Group 4 

Run 1 M30B Start 

4/15/2010 8:57 

End 4/14/2010 

10:57

0

33 Unit Net Electric Generation 376 MWh BHS3 Group 4 

Run 1 M30B Start 

4/15/2010 8:57 

End 4/14/2010 

10:57

0

33 Sorbent Injection Rate 35.5 lb/hr BHS3 Group 4 

Run 1 M30B Start 

4/15/2010 8:57 

End 4/14/2010 

10:57

0

34 Coal Burned 0.213 1000 Tons/hr BHS3 Group 4 

Run 2 M29 Start 

4/15/2010 9:21 

End 4/14/2010 

13:38

0

34 Unit Gross Electrical Output 401 Mwe BHS3 Group 4 

Run 2 M29 Start 

4/15/2010 9:21 

End 4/14/2010 

13:38

0

34 Unit Net Electric Generation 386 MWh BHS3 Group 4 

Run 2 M29 Start 

4/15/2010 9:21 

End 4/14/2010 

13:38

0

Tuesday, February 22, 2011 Page 28 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

34 Sorbent Injection Rate 35.6 lb/hr BHS3 Group 4 

Run 2 M29 Start 

4/15/2010 9:21 

End 4/14/2010 

13:38

0

35 Coal Burned 0.21 1000 Tons/hr BHS3 Group 4 

Run 2 

OTM027/028 Start 

4/15/2010 8:45 

End 4/14/2010 

15:57

0

35 Unit Gross Electrical Output 396 Mwe BHS3 Group 4 

Run 2 

OTM027/028 Start 

4/15/2010 8:45 

End 4/14/2010 

15:57

0

35 Unit Net Electric Generation 380 MWh BHS3 Group 4 

Run 2 

OTM027/028 Start 

4/15/2010 8:45 

End 4/14/2010 

15:57

0

35 Sorbent Injection Rate 35.6 lb/hr BHS3 Group 4 

Run 2 

OTM027/028 Start 

4/15/2010 8:45 

End 4/14/2010 

15:57

0

36 Coal Burned 0.212 1000 Tons/hr BHS3 Group 4 

Run 2 M30B Start 

4/15/2010 12:11 

End 4/14/2010 

14:11

0

36 Unit Gross Electrical Output 401 Mwe BHS3 Group 4 

Run 2 M30B Start 

4/15/2010 12:11 

End 4/14/2010 

14:11

0

36 Unit Net Electric Generation 386 MWh BHS3 Group 4 

Run 2 M30B Start 

4/15/2010 12:11 

End 4/14/2010 

14:11

0

36 Sorbent Injection Rate 35.6 lb/hr BHS3 Group 4 

Run 2 M30B Start 

4/15/2010 12:11 

End 4/14/2010 

14:11

0

Tuesday, February 22, 2011 Page 29 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

37 Coal Burned 0.212 1000 Tons/hr BHS3 Group 4 

Run 3 M29 Start 

4/15/2010 17:47 

End 4/14/2010 

22:12

0

37 Unit Gross Electrical Output 401 Mwe BHS3 Group 4 

Run 3 M29 Start 

4/15/2010 17:47 

End 4/14/2010 

22:12

0

37 Unit Net Electric Generation 386 MWh BHS3 Group 4 

Run 3 M29 Start 

4/15/2010 17:47 

End 4/14/2010 

22:12

0

37 Sorbent Injection Rate 35.6 lb/hr BHS3 Group 4 

Run 3 M29 Start 

4/15/2010 17:47 

End 4/14/2010 

22:12

0

38 Coal Burned 0.212 1000 Tons/hr BHS3 Group 4 

Run 3 

OTM027/028 Start 

4/15/2010 16:40 

End 4/16/2010 

0:13

0

38 Unit Gross Electrical Output 401 Mwe BHS3 Group 4 

Run 3 

OTM027/028 Start 

4/15/2010 16:40 

End 4/16/2010 

0:13

0

38 Unit Net Electric Generation 386 MWh BHS3 Group 4 

Run 3 

OTM027/028 Start 

4/15/2010 16:40 

End 4/16/2010 

0:13

0

38 Sorbent Injection Rate 35.6 lb/hr BHS3 Group 4 

Run 3 

OTM027/028 Start 

4/15/2010 16:40 

End 4/16/2010 

0:13

0

39 Coal Burned 0.211 1000 Tons/hr BHS3 Group 4 

Run 3 M30B Start 

4/15/2010 16:00 

End 4/14/2010 

18:00

0

Tuesday, February 22, 2011 Page 30 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

39 Unit Gross Electrical Output 401 Mwe BHS3 Group 4 

Run 3 M30B Start 

4/15/2010 16:00 

End 4/14/2010 

18:00

0

39 Unit Net Electric Generation 386 MWh BHS3 Group 4 

Run 3 M30B Start 

4/15/2010 16:00 

End 4/14/2010 

18:00

0

39 Sorbent Injection Rate 35.6 lb/hr BHS3 Group 4 

Run 3 M30B Start 

4/15/2010 16:00 

End 4/14/2010 

18:00

0

1 Coal Burned 0.212 1000 Tons/hr BHS3 Group 1 

Run 1M0010 Start 

4/16/2010 11:10 

End 4/16/2010 

13:25

0

2 Coal Burned 0.212 1000 Tons/hr BHS3 Group 1 

Runs 1-4 M0031 

Start 4/16/2010 

11:20 End 

4/16/2010 13:21

11:20End 

4/16/2010

13:21

0

3 Coal Burned 0.211 1000 Tons/hr BHS3 Group 1 

Run 1 M18 (CH4) 

Start 4/16/2010 

18:10 End 

4/16/2010 18:12

0

4 Coal Burned 0.211 1000 Tons/hr BHS3 Group 1 

Run 1 M6C (SO2) 

Start 4/16/2010 

11:10 End 

4/16/2010 13:09

0

5 Coal Burned 0.211 1000 Tons/hr BHS3 Group 1 

Run 1 M10 (CO) 

Start 4/16/2010 

11:10 End 

4/16/2010 13:09

0

1 Unit Gross Electrical Output 398 Mwe BHS3 Group 1 

Run 1M0010 Start 

4/16/2010 11:10 

End 4/16/2010 

13:25

0

Tuesday, February 22, 2011 Page 31 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

4 Unit Gross Electrical Output 398 Mwe BHS3 Group 1 

Run 1 M6C (SO2) 

Start 4/16/2010 

11:10 End 

4/16/2010 13:09

0

5 Unit Gross Electrical Output 398 Mwe BHS3 Group 1 

Run 1 M10 (CO) 

Start 4/16/2010 

11:10 End 

4/16/2010 13:09

0

1 Unit Net Electric Generation 382 MWh BHS3 Group 1 

Run 1M0010 Start 

4/16/2010 11:10 

End 4/16/2010 

13:25

0

4 Unit Net Electric Generation 382 MWh BHS3 Group 1 

Run 1 M6C (SO2) 

Start 4/16/2010 

11:10 End 

4/16/2010 13:09

0

5 Unit Net Electric Generation 382 MWh BHS3 Group 1 

Run 1 M10 (CO) 

Start 4/16/2010 

11:10 End 

4/16/2010 13:09

0

6 Coal Burned 0.211 1000 Tons/hr BHS3 Group 1 

Run 1 M25A 

(TOC as propane) 

Start 4/16/2010 

11:10 End 

4/16/2010 13:09

0

6 Unit Gross Electrical Output 398 Mwe BHS3 Group 1 

Run 1 M25A 

(TOC as propane) 

Start 4/16/2010 

11:10 End 

4/16/2010 13:09

0

6 Unit Net Electric Generation 382 MWh BHS3 Group 1 

Run 1 M25A 

(TOC as propane) 

Start 4/16/2010 

11:10 End 

4/16/2010 13:09

0

7 Coal Burned 0.211 1000 Tons/hr BHS3 Group 1 

Run 2 M0010 

Start 4/16/2010 

14:16 End 

4/16/2010 16:34

0

Tuesday, February 22, 2011 Page 32 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

APCD Run Data

Process Lab Run Data

7 Unit Gross Electrical Output 398 Mwe BHS3 Group 1 

Run 2 M0010 

Start 4/16/2010 

14:16 End 

4/16/2010 16:34

0

7 Unit Net Electric Generation 383 MWh BHS3 Group 1 

Run 2 M0010 

Start 4/16/2010 

14:16 End 

4/16/2010 16:34

0

8 Coal Burned 0.211 1000 Tons/hr BHS3 Group 1 

Run 2 M0011 

Start 4/16/2010 

14:16 End 

4/16/2010 16:34

0

8 Unit Gross Electrical Output 398 Mwe BHS3 Group 1 

Run 2 M0011 

Start 4/16/2010 

14:16 End 

4/16/2010 16:34

0

8 Unit Net Electric Generation 383 MWh BHS3 Group 1 

Run 2 M0011 

Start 4/16/2010 

14:16 End 

4/16/2010 16:34

0

9 Coal Burned 0.211 1000 Tons/hr BHS3 Group 1 

Runs 5-8 M0031 

Start 4/16/2010 

14:23 End 

4/16/2010 16:32

0

9 Unit Gross Electrical Output 398 Mwe BHS3 Group 1 

Runs 5-8 M0031 

Start 4/16/2010 

14:23 End 

4/16/2010 16:32

0

9 Unit Net Electric Generation 383 MWh BHS3 Group 1 

Runs 5-8 M0031 

Start 4/16/2010 

14:23 End 

4/16/2010 16:32

0

Run Name Value UOM Comments

Target

Value

1 ELECTROSTATIC PRECIPITATOR (CD2) 0 0

1 BAGHOUSE (CD3) 0 0

1 ACTIVATED CARBON ADSORPTION (CD4) 0 0

Tuesday, February 22, 2011 Page 33 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

Run Name Value UOM Comments

1 Fuel Higher Heating Value 0 Btu/lb

2 Fuel Higher Heating Value 0 Btu/lb

1 Fuel Moisture 0 %

2 Fuel Moisture 0 %

1 Fuel Mercury Content 0 ppm

2 Fuel Mercury Content 0 ppm

1 Fuel Cadmium Content 0 ppm

2 Fuel Cadmium Content 0 ppm

1 Ultimate/Proximate Analysis 0

2 Ultimate/Proximate Analysis 0

1 Fuel Nickel Content 0 ppm

2 Fuel Nickel Content 0 ppm

1 Fuel Arsenic Content 0 ppm

2 Fuel Arsenic Content 0 ppm

1 Fuel Chromium Content 0 ppm

2 Fuel Chromium Content 0 ppm

1 Fuel Beryllium Content 0 ppm

2 Fuel Beryllium Content 0 ppm

1 Fuel Lead Content 0 ppm

2 Fuel Lead Content 0 ppm

1 Fuel Manganese Content 0 ppm

2 Fuel Manganese Content 0 ppm

1 Fuel Chlorine Content 0 ppm

2 Fuel Chlorine Content 0 ppm

1 Fuel Fluorine Content 0 ppm

2 Fuel Fluorine Content 0 ppm

Tuesday, February 22, 2011 Page 34 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

Sampling / Stack Data Results Detail

Location Stack Exit - Method 0011

Average

Run Number 1-1 1-2 1-3

Test Date 4/16/2010 4/16/2010 4/16/2010

Run Start Time 11:10:00 AM 2:16:00 PM 5:23:00 PM

Run Finish Time 1:25:00 PM 4:34:00 PM 7:50:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 120 120 120

Nozzle Diameter, inches 0.193 0.193 0.193 0.193

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.0469 1.0469 1.0469 1.047

Barometric Pressure, inches of Mercury 29.865 29.6 29.565 29.677

Average Orifice Meter Differential, inches H2O 1.37 1.39 1.30 1.353

Dry Gas Meter Volume Sampled, cubic feet 71.789 70.698 70.091 70.859

Average Dry Gas Meter Temperature, °F 58.42 55.79 56.83 57.013

Dry Gas Meter Volume Sampled, dscf 76.662 75.214 74.314 75.397

Total Moisture Liquid collected, g 225.2 223.6 224.7 224.500

Volume of Water Vapor, standard cubic feet 10.60 10.52 10.58 10.567

Moisture Content of Stack Gas, % 12.15 12.27 12.46 12.293

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

Dry Mole Fraction 0.8785 0.8773 0.8754 0.877

Carbon Dioxide, % 15.5 15.3 15.2 15.333

Oxygen, % 4.2 4.3 4.3 4.267

Carbon Monoxide & Nitrogen, % 80.3 80.4 80.5 80.400

Fuel Factor 1.08 1.08 1.09

Dry Molecular Weight, lb/lb-Mole 30.65 30.62 30.60 30.623

Wet Molecular weight, lb/lb-Mole 29.11 29.07 29.03 29.070

Flue Gas Static Pressure, inches of H2O 2.1 2 2 2.033

Absolute Flue Gas Pressure, inches of Mercury 30.02 29.75 29.71 29.827

Average Stack Gas Temperature, °F 293.00 293.83 294.08 293.637

Average Velocity Head, inches of H2O 1.6646558369

1274

1.606933558

62099

1.582094579

58215

1.618

Average Stack Gas Velocity, feet/second 86.01 84.99 84.46 85.153

Stack Cross-Sectional Area, square feet 268.687 268.687 268.687 268.687

Dry Volumetric Flow Rate, dry scfm 856,991.8 837,143.2 828,730.0 840,955.000

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,386,586.1 1,370,142.5 1,361,598.2 1,372,775.6

00

Percent Isokinetic of Sampling Rate, % 98.6 99.0 98.8 98.800

Percent Excess Air, % 24.7 25.4 25.4 25.167

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Round Duct Diameter, inches 18.5 18.5 18.5

Rectangular Duct Width, inches 196.7 196.7 196.7

Rectangular Duct Length, inches 196.7 196.7 196.7

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Tuesday, February 22, 2011 Page 35 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

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

Tuesday, February 22, 2011 Page 36 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

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

Tuesday, February 22, 2011 Page 37 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

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

Tuesday, February 22, 2011 Page 38 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

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

Tuesday, February 22, 2011 Page 39 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

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

Tuesday, February 22, 2011 Page 40 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

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

Tuesday, February 22, 2011 Page 41 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

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

Tuesday, February 22, 2011 Page 42 of 42
Bridgeport Unit 3 EGU ICR MACT

8/13/2010

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

Tuesday, February 22, 2011 Page 43 of 42