Name: Philip Fontenelle

Title: Environmental Manager

Company: Logan Generating Company L.P.

Sign Date: 9/2/2010

Name: Lenny D. Katerynczuk

Title: Project Manager

Company: AirNova, Inc.

Sign Date: 9/2/2010

Permitted Facility Representative / Date Testing Company Representative / Date

MACT HAP EDR Logan Generating

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.

Thursday, February 03, 2011 Page 1 of 25
MACT HAP EDR Logan Generating

9/2/2010

Facility Information:

Logan Generating Company

76 Route 130

Swedesboro NJ 08085

Contact: Phillip Fontenelle

Phone: 856-241-4575

Fax: 856-467-5256

Email: PhilFontenelle@cogentrix.com

Testing Company:

Air Nova Inc.

585 Clayton Avenue

Pennsauken NJ 08019

Contact:Lenny Katerynczuk

Phone: 856-486-1500

Fax: 856-486-9896

Email: Lenny@airnova.com

Air Permit Number:

10043

Permitted Source ID/Name:

1001 PC Boiler

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

225 MW

Target Process Test Rate

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

 process flow diagram:

The Logan Generating plant uses bituminous pulverzized coal. The coal is burned in low nox burners utilizing 

overfire air. A selective catalytic reducer uses ammonia to reduce Nox. The flue gas then passes through an air 

preheater, spray dry absorber to reduce Sox, and fabric baghouse.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 3401500357 FRS #: 110000575182

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 168 0 0 0 2112 1464 4 12

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

Thursday, February 03, 2011 Page 2 of 25
MACT HAP EDR Logan Generating

9/2/2010

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

Stack Exit Total PCBs Method 23 3 480 0

Stack Exit Total TEQ Method 23 3 480 0

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 3 120 0

Stack Exit Hydrogen Chloride Method 26 3 180 0

Stack Exit Hydrogen Fluoride Method 26 3 180 0

Hydrogen Chloride Method 26A 3 180 0 run date is 3/8 not 

4/10 - ERT entry error

Stack Exit

Hydrogen Fluoride Method 26A 3 180 0 run date is 3/8 not 

4/10 - ERT entry error

Stack Exit

Inorganic (Aqueous) 

Condensible Part.

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Thursday, February 03, 2011 Page 3 of 25
MACT HAP EDR Logan Generating

9/2/2010

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.

See attached test report

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

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Stack Exit Arsenic Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Selenium Method 29 3 240 0

Stack Exit Chromium Method 29 3 240 0

Stack Exit Cadmium Method 29 3 240 0

Stack Exit Lead Method 29 3 240 0

Stack Exit Beryllium Method 29 3 240 0

Stack Exit Antimony Method 29 3 240 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 3 240 0

Stack Exit O2 Method 3A O2 3 480 0

Stack Exit Co2 Method 3A CO2 3 480 0

Stack Exit O2 Method 3A O2 3 120 0

Organic Condensible 

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

Total 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

Thursday, February 03, 2011 Page 4 of 25
MACT HAP EDR Logan Generating

9/2/2010

Sampling / Stack Data Results Summary

Location Stack Exit - Method 0011

Average

Run Number 1 2 3

Test Date 4/8/2010 4/8/2010 4/8/2010

Run Start Time 7:56:00 AM 11:50:00 

AM

3:52:00 PM

Run Finish Time 10:09:00 AM 2:00:00 PM 6:00:00 PM

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 73.957 74.066 73.653 73.892

Moisture Content of Stack Gas, % 11.70 11.52 12.61 11.943

Moisture Saturation at Stack Gas Temperature, % 50.41 50.97 52.48 51.287

Carbon Dioxide, % 13.81 14.05 14.11 13.990

Oxygen, % 5.09 5.23 5.13 5.150

Average Stack Gas Temperature, °F 179.00 179.42 180.58 179.667

Dry Volumetric Flow Rate, dry scfm 536,596.3 532,962.8 527,334.8 532,297.967

Actual Wet Volumetric Flue Gas Flow Rate, acfm 743,151.1 738,348.2 743,520.5 741,673.267

Percent Isokinetic of Sampling Rate, % 94.7 95.5 95.0 95.067

F-Factor, dscfm/MMBtu @ %O2 7885 9533 9537 8,985.000

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

Thursday, February 03, 2011 Page 5 of 25
MACT HAP EDR Logan Generating

9/2/2010

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

Thursday, February 03, 2011 Page 6 of 25
MACT HAP EDR Logan Generating

9/2/2010

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

Thursday, February 03, 2011 Page 7 of 25
MACT HAP EDR Logan Generating

9/2/2010

Location Stack Exit - Method 7E

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack Exit - 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

Thursday, February 03, 2011 Page 8 of 25
MACT HAP EDR Logan Generating

9/2/2010

Emissions Summary

Location: Stack Exit - Method 0011

Compound: Formaldehyde

Average

RunNumber 1 2 3

Mass_mg 0.00242 0.00204 0.0022 0.002

Elb/hr 2.32E-03 1.94E-03 2.08E-03 0.002

gr/dscf 5.05E-07 4.25E-07 4.61E-07 0.000

lb/mmBtuO2 7.52E-07 7.72E-07 8.32E-07 0.000

mg/dscm 1.16E-03 9.73E-04 1.06E-03 0.001

ppm 9.26E-04 7.79E-04 8.45E-04 0.001

ppm@7%O2 8.14E-04 6.91E-04 7.45E-04 0.001

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 3.82E-02 3.21E-02 5.34E-02 0.041

ppm 5.04E+01 3.47E+01 5.82E+01 47.767

ppm@7%O2 4.43E+01 3.08E+01 5.13E+01 42.133

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

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

gr/dscf 4.77E-05 2.95E-04 1.25E-04 0.000

lb/mmBtuO2 7.10E-05 5.36E-04 2.26E-04 0.000

mg/dscm 1.09E-01 6.75E-01 2.86E-01 0.357

ppm 5.95E-02 3.68E-01 1.56E-01 0.195

ppm@7%O2 5.23E-02 3.26E-01 1.38E-01 0.172

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 0.05 0.06 0.06 0.057

Elb/hr 3.04E-02 3.59E-02 3.55E-02 0.034

lb/mmBtuO2 9.96E-06 1.46E-05 1.41E-05 0.000

mg/dscm 1.53E-02 1.83E-02 1.79E-02 0.017

mg/dscm@7%O2 1.35E-02 1.62E-02 1.58E-02 0.015

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.03 0.04 0.04 0.037

Elb/hr 1.82E-02 2.39E-02 2.36E-02 0.022

lb/mmBtuO2 5.97E-06 9.71E-06 9.40E-06 0.000

mg/dscm 9.18E-03 1.22E-02 1.19E-02 0.011

mg/dscm@7%O2 8.07E-03 1.08E-02 1.05E-02 0.010

Thursday, February 03, 2011 Page 9 of 25
MACT HAP EDR Logan Generating

9/2/2010

Location: Stack Exit - Method 29 

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.000171 0.0001 0.0001 0.000

Elb/hr 6.80E-05 3.37E-05 2.55E-05 0.000

lb/mmBtuO2 2.83E-08 1.41E-08 1.04E-08 0.000

mg/dscm 3.55E-05 1.77E-05 1.30E-05 0.000

mg/dscm@7%O2 3.16E-05 1.57E-05 1.16E-05 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.000614 0.001643 0.000604 0.001

Elb/hr 2.44E-04 5.53E-04 1.54E-04 0.000

lb/mmBtuO2 1.02E-07 2.31E-07 6.29E-08 0.000

mg/dscm 1.28E-04 2.91E-04 7.87E-05 0.000

mg/dscm@7%O2 1.14E-04 2.58E-04 7.00E-05 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.000048 0.000046 0.000025 0.000

Elb/hr 1.91E-05 1.55E-05 6.37E-06 0.000

lb/mmBtuO2 7.95E-09 6.47E-09 2.60E-09 0.000

mg/dscm 9.98E-06 8.15E-06 3.26E-06 0.000

mg/dscm@7%O2 8.87E-06 7.24E-06 2.90E-06 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.000383 0.000155 0.000171 0.000

Elb/hr 1.52E-04 5.22E-05 4.36E-05 0.000

lb/mmBtuO2 6.34E-08 2.18E-08 1.78E-08 0.000

mg/dscm 7.96E-05 2.75E-05 2.23E-05 0.000

mg/dscm@7%O2 7.07E-05 2.44E-05 1.98E-05 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.002792 0.00266 0.001858 0.002

Elb/hr 1.11E-03 8.95E-04 4.74E-04 0.001

lb/mmBtuO2 4.62E-07 3.74E-07 1.94E-07 0.000

mg/dscm 5.80E-04 4.71E-04 2.42E-04 0.000

mg/dscm@7%O2 5.15E-04 4.18E-04 2.15E-04 0.000

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.001604 0.001393 0.000898 0.001

Elb/hr 6.38E-04 4.69E-04 2.29E-04 0.000

lb/mmBtuO2 2.66E-07 1.96E-07 9.35E-08 0.000

mg/dscm 3.33E-04 2.47E-04 1.17E-04 0.000

Thursday, February 03, 2011 Page 10 of 25
MACT HAP EDR Logan Generating

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mg/dscm@7%O2 2.96E-04 2.19E-04 1.04E-04 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.00504 0.002576 0.001768 0.003

Elb/hr 2.01E-03 8.67E-04 4.51E-04 0.001

lb/mmBtuO2 8.34E-07 3.62E-07 1.84E-07 0.000

mg/dscm 1.05E-03 4.57E-04 2.30E-04 0.001

mg/dscm@7%O2 9.33E-04 4.06E-04 2.05E-04 0.001

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.003128 0.003616 0.002922 0.003

Elb/hr 1.24E-03 1.22E-03 7.45E-04 0.001

lb/mmBtuO2 5.18E-07 5.08E-07 3.04E-07 0.000

mg/dscm 6.50E-04 6.41E-04 3.81E-04 0.001

mg/dscm@7%O2 5.78E-04 5.69E-04 3.39E-04 0.000

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.0001 0.0001 0.0001 0.000

Elb/hr 3.98E-05 3.37E-05 2.55E-05 0.000

lb/mmBtuO2 1.66E-08 1.41E-08 1.04E-08 0.000

mg/dscm 2.08E-05 1.77E-05 1.30E-05 0.000

mg/dscm@7%O2 1.85E-05 1.57E-05 1.16E-05 0.000

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

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

lb/mmBtuO2 7.69E-02 1.06E-01 8.98E-02 0.091

mg/dscm 1.18E+02 1.35E+02 1.14E+02 122.333

mg/dscm@7%O2 1.04E+02 1.19E+02 1.00E+02 107.667

ppm 4.44E+01 5.06E+01 4.27E+01 45.900

ppm@7%O2 3.90E+01 4.46E+01 3.76E+01 40.400

Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

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

lb/mmBtuO2 1.05E-01 1.26E-01 1.30E-01 0.120

mg/dscm 1.62E+02 1.58E+02 1.65E+02 161.667

mg/dscm@7%O2 1.42E+02 1.40E+02 1.45E+02 142.333

ppm 8.46E+01 8.26E+01 8.62E+01 84.467

ppm@7%O2 7.44E+01 7.33E+01 7.60E+01 74.567

Location: Stack Exit - OTM - 27/28

Thursday, February 03, 2011 Page 11 of 25
MACT HAP EDR Logan Generating

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Process Run Data

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 2.4 5.1 1 2.833

lb/mmBtuO2 6.23E-04 1.12E-03 2.21E-04 0.001

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 2.4 5.1 1 2.833

lb/mmBtuO2 6.23E-04 1.12E-03 2.21E-04 0.001

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 38.6 54.1 47 46.567

lb/mmBtuO2 1.00E-02 1.19E-02 1.04E-02 0.011

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 2.1 1 1.8 1.633

lb/mmBtuO2 5.45E-04 2.19E-04 3.97E-04 0.000

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 43.1 60.2 49.8 51.033

lb/mmBtuO2 1.12E-02 1.32E-02 1.10E-02 0.012

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 43.1 60.2 49.8 51.033

lb/mmBtuO2 1.12E-02 1.32E-02 1.10E-02 0.012

Thursday, February 03, 2011 Page 12 of 25
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Process Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input 1729.9 Million Btus/hr 0 4/6/10

2 Heat Input 1786.7 Million Btus/hr 0 4/7/10

3 Heat Input 1524.3 Million Btus/hr 0 4/8/10

1 Average Heat Input 1729.9 MMBtu/hr 0 4/6/10

2 Average Heat Input 1786.7 MMBtu/hr 0 4/7/10

3 Average Heat Input 1524.3 MMBtu/hr 0 4/8/10

1 Steam Output 1276.8 1000 lb steam/hr 0 4/6/10

2 Steam Output 1314.9 1000 lb steam/hr 0

3 Steam Output 1145.9 1000 lb steam/hr 0 4/8/10

1 Synfuel Firing Rate 0 0

2 Synfuel Firing Rate 0 0

3 Synfuel Firing Rate 0 0

1 Petroleum Coke Firing Rate 0 0

2 Petroleum Coke Firing Rate 0 0

3 Petroleum Coke Firing Rate 0 0

1 Coal Gas Firing Rate 0 0

2 Coal Gas Firing Rate 0 0

3 Coal Gas Firing Rate 0 0

1 Fuel Oil Firing Rate 0.98 0 gpm

2 Fuel Oil Firing Rate 0.55 0 gpm

3 Fuel Oil Firing Rate 1.28 0 gpm

1 Flue Gas Flow Rate dscfm 0 see individual runs

2 Flue Gas Flow Rate dscfm 0 see individual runs

3 Flue Gas Flow Rate 0 dscfm 0 see individual runs

1 Pressure Drop Across FGD (if applicable) 4.32 in H20 0

2 Pressure Drop Across FGD (if applicable) 4.32 in H20 0

3 Pressure Drop Across FGD (if applicable) 4.19 in H20 0

1 FGD Scrubber Liquor pH 0 pH not applicable - 

spray dryer 

absorber

0

2 FGD Scrubber Liquor pH 0 pH not applicable - 

spray dryer 

absorber

0

Thursday, February 03, 2011 Page 13 of 25
MACT HAP EDR Logan Generating

9/2/2010

3 FGD Scrubber Liquor pH 0 pH not applicable - 

spray dryer 

absorber

0

1 FGD Scrubber Liquor Flow Rate 154.9 gal/min 0

2 FGD Scrubber Liquor Flow Rate 156.87 gal/min 0

3 FGD Scrubber Liquor Flow Rate 141.94 gal/min 0

1 Sorbent Type and Sorbent Injection Rate (if 

applicable)

lb/hr 0 limestone

2 Sorbent Type and Sorbent Injection Rate (if 

applicable)

lb/hr 0 limestone

3 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0 Limestone

1 Flue Gas Oxygen Content 7.49 % 0 wet

2 Flue Gas Oxygen Content 7.19 % 0 wet, avg 4/7/10

3 Flue Gas Oxygen Content 8.11 % 0 wet, avg 4/8/10

1 Flue Gas Carbon Dioxide Content % 0 wet

2 Flue Gas Carbon Dioxide Content % 0 wet, avg 4/7/10

3 Flue Gas Carbon Dioxide Content % 0

1 Flue Gas Moisture Content % 0

2 Flue Gas Moisture Content % 0

3 Flue Gas Moisture Content % 0

1 Flue Gas Sampling Point Temperature 176.3 Deg F 0 avg 4/6/10

2 Flue Gas Sampling Point Temperature 181.63 Deg F 0

3 Flue Gas Sampling Point Temperature 180.51 Deg F 0 avg 4/8/10

1 Flue Gas Pressure 28.3 in. Hg 29.89

2 Flue Gas Pressure 28.32 in. Hg 29.89

3 Flue Gas Pressure 28.44 in. Hg 29.89

1 Standard Pressure 29.92 in. Hg 0

2 Standard Pressure 29.92 in. Hg 0

3 Standard Pressure 29.92 in. Hg 0

1 Standard Temperature 68 Deg F 0

2 Standard Temperature 68 Deg F 0

3 Standard Temperature 68 Deg F 0

1 Unit Gross Electrical Output 170.71 MW 0

2 Unit Gross Electrical Output 194.73 MW 0

3 Unit Gross Electrical Output 167.61 MW 0

1 Unit Net Electric Generation MWh 0

2 Unit Net Electric Generation MWh 0 4/7/10

Thursday, February 03, 2011 Page 14 of 25
MACT HAP EDR Logan Generating

9/2/2010

APCD Run Data

Process Lab Run Data

3 Unit Net Electric Generation MWh 0

Run Name Value UOM Comments

Target

Value

1 LOW NOX BURNERS 1 N/A 1

1 OVERFIRE AIR 1 N/A 1

1 SCR (SELECTIVE CATALYTIC REDUCTION) 1 1

1 SPRAY DRYER 1 1

1 BAGHOUSE 1 1

Run Name Value UOM Comments

1 Fuel Higher Heating Value 12850 Btu/lb

2 Fuel Higher Heating Value 13118 Btu/lb

3 Fuel Higher Heating Value 13370 Btu/lb

1 Fuel Moisture 3.44 %

2 Fuel Moisture 3.47 %

3 Fuel Moisture 2.83 %

1 Fuel Mercury Content ppm

2 Fuel Mercury Content ppm

3 Fuel Mercury Content ppm

1 Fuel Cadmium Content ppm

2 Fuel Cadmium Content ppm

3 Fuel Cadmium Content ppm

1 Ultimate/Proximate Analysis 0

2 Ultimate/Proximate Analysis 0

3 Ultimate/Proximate Analysis 0

1 Fuel Nickel Content ppm

2 Fuel Nickel Content ppm

3 Fuel Nickel Content ppm

1 Fuel Arsenic Content ppm

2 Fuel Arsenic Content ppm

3 Fuel Arsenic Content ppm

1 Fuel Chromium Content ppm

2 Fuel Chromium Content ppm

3 Fuel Chromium Content ppm

1 Fuel Beryllium Content ppm

2 Fuel Beryllium Content ppm

3 Fuel Beryllium Content ppm

1 Fuel Lead Content ppm

Thursday, February 03, 2011 Page 15 of 25
MACT HAP EDR Logan Generating

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2 Fuel Lead Content ppm

3 Fuel Lead Content ppm

1 Fuel Manganese Content ppm

2 Fuel Manganese Content ppm

3 Fuel Manganese Content ppm

1 Fuel Chlorine Content 1200 ppm

2 Fuel Chlorine Content 1100 ppm

3 Fuel Chlorine Content 1100 ppm

1 Fuel Fluorine Content 59 ppm

2 Fuel Fluorine Content 64 ppm

3 Fuel Fluorine Content 43 ppm

4 Fuel Higher Heating Value 13119 Btu/lb

4 Fuel Moisture 3.55 %

4 Fuel Mercury Content 0.12 ppm

4 Fuel Cadmium Content 0 ppm

4 Ultimate/Proximate Analysis 0

4 Fuel Nickel Content 11 ppm

4 Fuel Arsenic Content ppm

4 Fuel Chromium Content 19 ppm

4 Fuel Beryllium Content 1.8 ppm

4 Fuel Lead Content 7 ppm

4 Fuel Manganese Content 6 ppm

4 Fuel Chlorine Content 1100 ppm

4 Fuel Fluorine Content 61 ppm

5 Fuel Higher Heating Value 13219 Btu/lb

5 Fuel Moisture 3.63 %

5 Fuel Mercury Content 0.09 ppm

5 Fuel Cadmium Content 0 ppm

5 Ultimate/Proximate Analysis 0

5 Fuel Nickel Content 12 ppm

5 Fuel Arsenic Content ppm

5 Fuel Chromium Content 17 ppm

5 Fuel Beryllium Content 1.7 ppm

5 Fuel Lead Content 7 ppm

5 Fuel Manganese Content 8 ppm

5 Fuel Chlorine Content 1200 ppm

5 Fuel Fluorine Content 61 ppm

6 Fuel Higher Heating Value 13108 Btu/lb

6 Fuel Moisture 3.85 %

6 Fuel Mercury Content 0.09 ppm

6 Fuel Cadmium Content 0 ppm

6 Ultimate/Proximate Analysis 0

6 Fuel Nickel Content 11 ppm

Thursday, February 03, 2011 Page 16 of 25
MACT HAP EDR Logan Generating

9/2/2010

6 Fuel Arsenic Content ppm

6 Fuel Chromium Content 17 ppm

6 Fuel Beryllium Content 1.6 ppm

6 Fuel Lead Content 7 ppm

6 Fuel Manganese Content 10 ppm

6 Fuel Chlorine Content 1000 ppm

6 Fuel Fluorine Content 62 ppm

Thursday, February 03, 2011 Page 17 of 25
MACT HAP EDR Logan Generating

9/2/2010

Sampling / Stack Data Results Detail

Location Stack Exit - Method 0011

Average

Run Number 1 2 3

Test Date 4/8/2010 4/8/2010 4/8/2010

Run Start Time 7:56:00 AM 11:50:00 AM 3:52:00 PM

Run Finish Time 10:09:00 AM 2:00:00 PM 6:00:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 120 120 120

Nozzle Diameter, inches 0.185 0.185 0.186 0.185

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.02 1.02 1.02 1.020

Barometric Pressure, inches of Mercury 29.73 29.68 29.58 29.663

Average Orifice Meter Differential, inches H2O 1.25 1.24 1.24 1.243

Dry Gas Meter Volume Sampled, cubic feet 74.428 74.715 74.694 74.612

Average Dry Gas Meter Temperature, °F 80.21 80.58 81.63 80.807

Dry Gas Meter Volume Sampled, dscf 73.957 74.066 73.653 73.892

Total Moisture Liquid collected, g 208.3 204.7 225.8 212.933

Volume of Water Vapor, standard cubic feet 9.80 9.64 10.63 10.023

Moisture Content of Stack Gas, % 11.70 11.52 12.61 11.943

Moisture Saturation at Stack Gas Temperature, % 50.41 50.97 52.48 51.287

Dry Mole Fraction 0.883 0.8848 0.8739 0.881

Carbon Dioxide, % 13.81 14.05 14.11 13.990

Oxygen, % 5.09 5.23 5.13 5.150

Carbon Monoxide & Nitrogen, % 81.1 80.72 80.76 80.860

Fuel Factor 1.14 1.12 1.12

Dry Molecular Weight, lb/lb-Mole 30.41 30.46 30.46 30.443

Wet Molecular weight, lb/lb-Mole 28.96 29.02 28.89 28.957

Flue Gas Static Pressure, inches of H2O -1.7 -1.7 -1.7 -1.700

Absolute Flue Gas Pressure, inches of Mercury 29.61 29.56 29.46 29.543

Average Stack Gas Temperature, °F 179.00 179.42 180.58 179.667

Average Velocity Head, inches of H2O 1.6846363785

3695

1.662376744

72731

1.669749620

20747

1.672

Average Stack Gas Velocity, feet/second 80.46 79.94 80.50 80.300

Stack Cross-Sectional Area, square feet 153.938 153.938 153.938 153.938

Dry Volumetric Flow Rate, dry scfm 536,596.3 532,962.8 527,334.8 532,297.967

Actual Wet Volumetric Flue Gas Flow Rate, acfm 743,151.1 738,348.2 743,520.5 741,673.267

Percent Isokinetic of Sampling Rate, % 94.7 95.5 95.0 95.067

Percent Excess Air, % 31.2 32.5 31.7 31.800

F-Factor, dscfm/MMBtu @ %O2 7885 9533 9537 8,985.000

Round Duct Diameter, inches 168 168 168

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Thursday, February 03, 2011 Page 18 of 25
MACT HAP EDR Logan Generating

9/2/2010

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

Thursday, February 03, 2011 Page 19 of 25
MACT HAP EDR Logan Generating

9/2/2010

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

Thursday, February 03, 2011 Page 20 of 25
MACT HAP EDR Logan Generating

9/2/2010

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

Thursday, February 03, 2011 Page 21 of 25
MACT HAP EDR Logan Generating

9/2/2010

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

Thursday, February 03, 2011 Page 22 of 25
MACT HAP EDR Logan Generating

9/2/2010

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

Thursday, February 03, 2011 Page 23 of 25
MACT HAP EDR Logan Generating

9/2/2010

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

Thursday, February 03, 2011 Page 24 of 25
MACT HAP EDR Logan Generating

9/2/2010

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

Thursday, February 03, 2011 Page 25 of 25