Name: John Stepan

Title: Engineer

Company: Air Compliance Consultants

Sign Date: 8/6/2010

Name: Rob Frey

Title: Vice President

Company: Air Compliance Consultants, Inc.

Sign Date: 8/6/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Hatfield Ferry Power Station

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.

Saturday, January 15, 2011 Page 1 of 21
Hatfield Ferry Power Station

8/6/2010

Facility Information:

Hatfields Ferry Power Station PA3179

2907 E. Roy Furman Highwaay

Masontown PA 15461

Contact: Mark A. Sowa

Phone: 724-838-6133

Fax:

Email: msowa@allegheny.com

Testing Company:

Air/Compliance Consultants, Inc.

1050 Wm Pitt Way

Pittsburgh PA 15238

Contact:Robert N. Frey

Phone: 412-826-3636

Fax: 412-826-3640

Email: rfrey@air-comp.com

Air Permit Number:

TV-30-00099

Permitted Source ID/Name:

Unit 1

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

550

Target Process Test Rate

495

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

 process flow diagram:

The Hatfield’s Ferry Power Station operates 3 coal-fired boilers (Units 031, 032, and 033) which generate electricity 

for sale and distribution. Each unit consists of a 570 megawatt (MW) Westinghouse generator driven by a 5,766 

million British thermal units per hour (MMBtu/hr) Babcock & Wilcox boiler retrofitted with low NOx cell burners. 

Each unit is also equipped with an electrostatic precipitator and a flue gas desulfurization system. The units exhaust 

to individual stacks contained within a concrete annul.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 110017437148 FRS #:

SCC / Description 10100224 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Spreader Stoker (Subbituminous 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

Unit 1 312 0 0 0 0 0 2 0

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Unit 1 Flowrate Method 1 - 4 3 120 0

Unit 1 % H2O Method 1 - 4 3 120 0

Unit 1 Carbon Monoxide Method 10 3 120 0

Unit 1 Formaldehyde Method 0011 3 120 0

Total organic compounds 

(TOC) as Propane

Unit 1 Method 25A 3 120 0

Saturday, January 15, 2011 Page 2 of 21
Hatfield Ferry Power Station

8/6/2010

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.

Unit 1 Hydrogen Chloride Method 26A 3 180 0

Unit 1 Hydrogen Fluoride Method 26A 3 180 0

Unit 1 Nickel Method 29 3 240 0

Unit 1 Manganese Method 29 3 240 0

Unit 1 Selenium Method 29 3 240 0

Unit 1 Antimony Method 29 3 240 0

Unit 1 Arsenic Method 29 3 240 0

Unit 1 Beryllium Method 29 3 240 0

Unit 1 Cadmium Method 29 3 240 0

Unit 1 Chromium Method 29 3 240 0

Unit 1 Cobalt Method 29 3 240 0

Unit 1 Lead Method 29 3 240 0

Inorganic (Aqueous) 

Condensible Part.

Unit 1 Method 5/OTM-28 3 240 0

Unit 1 Total Particulate Method 5/OTM-28 3 240 0

Organic Condensible 

Particulate

Unit 1 Method 5/OTM-28 3 240 0

Unit 1 Filterable Particulate Method 5/OTM-28 3 240 0

Unit 1 Sulfur Dioxide Method 6C 3 120 0

Unit 1 Nitrogen oxides (NOx) Method 7E 3 120 0

Saturday, January 15, 2011 Page 3 of 21
Hatfield Ferry Power Station

8/6/2010

Sampling / Stack Data Results Summary

Location Unit 1 - Method 0011

Average

Run Number 1 2 3

Test Date 5/12/2010 5/12/2010 5/12/2010

Run Start Time 7:10:00 AM 10:00:00 

AM

12:35:00 PM

Run Finish Time 9:21:00 AM 12:16:00 

PM

2:52:00 PM

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 72.165 75.005 74.103 73.758

Moisture Content of Stack Gas, % 15.09 14.24 15.65 14.993

Moisture Saturation at Stack Gas Temperature, % 14.93 15.11 15.74 15.260

Carbon Dioxide, % 14.81 14.73 14.58 14.707

Oxygen, % 4.62 4.7 4.72 4.680

Average Stack Gas Temperature, °F 128.63 129.08 130.63 129.447

Dry Volumetric Flow Rate, dry scfm 1,200,056.0 1,250,657.5 1,240,923.1 1,230,545.53

3

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,612,537.6 1,668,285.1 1,687,398.5 1,656,073.73

3

Percent Isokinetic of Sampling Rate, % 100.8 100.5 100.1 100.467

F-Factor, dscfm/MMBtu @ %O2 9796 9837 9720 9,784.333

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Unit 1 - 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

Saturday, January 15, 2011 Page 4 of 21
Hatfield Ferry Power Station

8/6/2010

Location Unit 1 - 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 Unit 1 - 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

Saturday, January 15, 2011 Page 5 of 21
Hatfield Ferry Power Station

8/6/2010

Location Unit 1 - 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 Unit 1 - Method 5/OTM-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

Saturday, January 15, 2011 Page 6 of 21
Hatfield Ferry Power Station

8/6/2010

Location Unit 1 - 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 Unit 1 - 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

Saturday, January 15, 2011 Page 7 of 21
Hatfield Ferry Power Station

8/6/2010

Emissions Summary

Location: Unit 1 - Method 0011

Compound: Formaldehyde

Average

RunNumber 1 2 3

Mass_mg 0.032 0.023 0.04 0.032

lb/mmBtuO2 1.23E-05 8.58E-06 1.49E-05 0.000

ppm 1.25E-02 8.67E-03 1.53E-02 0.012

ppm@7%O2 1.07E-02 7.44E-03 1.31E-02 0.010

Location: Unit 1 - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

ppm 4.75E+00 6.01E+00 6.30E+00 5.687

ppm@7%O2 4.06E+00 5.16E+00 5.41E+00 4.877

Location: Unit 1 - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 1.27E-03 4.91E-04 2.40E-04 0.001

ppm 8.82E-01 3.38E-01 1.66E-01 0.462

ppm@7%O2 7.53E-01 2.90E-01 1.43E-01 0.395

Location: Unit 1 - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 0.5 0.5 0.48 0.493

Elb/hr 7.69E-01 7.82E-01 7.58E-01 0.770

lb/mmBtuO2 1.32E-04 1.34E-04 1.27E-04 0.000

mg/dscm 1.68E-01 1.71E-01 1.63E-01 0.167

ppm 1.11E-01 1.13E-01 1.08E-01 0.111

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.25 0.29 0.33 0.290

Elb/hr 3.85E-01 4.53E-01 5.21E-01 0.453

lb/mmBtuO2 6.62E-05 7.79E-05 8.74E-05 0.000

mg/dscm 8.41E-02 9.92E-02 1.12E-01 0.098

ppm 1.01E-01 1.19E-01 1.35E-01 0.118

Location: Unit 1 - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.001 0.001 0.001 0.001

Elb/hr 1.15E-03 1.15E-03 1.12E-03 0.001

Saturday, January 15, 2011 Page 8 of 21
Hatfield Ferry Power Station

8/6/2010

lb/mmBtuO2 1.98E-07 2.02E-07 2.05E-07 0.000

ug/dscm 2.54E-01 2.60E-01 2.59E-01 0.258

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.0145 0.00676 0.00854 0.010

Elb/hr 1.67E-02 7.76E-03 9.54E-03 0.011

lb/mmBtuO2 2.87E-06 1.36E-06 1.75E-06 0.000

ug/dscm 3.68E+00 1.76E+00 2.21E+00 2.550

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.00021 0.00025 0.00025 0.000

Elb/hr 2.42E-04 2.87E-04 2.79E-04 0.000

lb/mmBtuO2 4.16E-08 5.05E-08 5.13E-08 0.000

ug/dscm 5.33E-02 6.50E-02 6.48E-02 0.061

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.00067 0.00056 0.00237 0.001

Elb/hr 7.72E-04 6.42E-04 2.65E-03 0.001

lb/mmBtuO2 1.33E-07 1.13E-07 4.86E-07 0.000

ug/dscm 1.70E-01 1.46E-01 6.14E-01 0.310

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.01108 0.02298 0.01904 0.018

Elb/hr 1.28E-02 2.64E-02 2.13E-02 0.020

lb/mmBtuO2 2.20E-06 4.64E-06 3.90E-06 0.000

ug/dscm 2.81E+00 5.98E+00 4.94E+00 4.577

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.00072 0.00102 0.00118 0.001

Elb/hr 8.29E-04 1.17E-03 1.32E-03 0.001

lb/mmBtuO2 1.43E-07 2.06E-07 2.42E-07 0.000

ug/dscm 1.83E-01 2.65E-01 3.06E-01 0.251

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.00344 0.00175 0.00243 0.003

Elb/hr 3.96E-03 2.01E-03 2.72E-03 0.003

lb/mmBtuO2 6.82E-07 3.53E-07 4.98E-07 0.000

ug/dscm 8.73E-01 4.55E-01 6.30E-01 0.653

Compound: Manganese

Average

RunNumber 1 2 3

Saturday, January 15, 2011 Page 9 of 21
Hatfield Ferry Power Station

8/6/2010

Mass_mg 0.0404 0.03075 0.3921 0.154

Elb/hr 4.65E-02 3.53E-02 4.38E-01 0.173

lb/mmBtuO2 8.00E-06 6.21E-06 8.04E-05 0.000

ug/dscm 1.03E+01 8.00E+00 1.02E+02 40.100

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.01701 0.04728 0.03096 0.032

Elb/hr 1.96E-02 5.42E-02 3.46E-02 0.036

lb/mmBtuO2 3.37E-06 9.54E-06 6.35E-06 0.000

ug/dscm 4.32E+00 1.23E+01 8.03E+00 8.217

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.1782 0.1399 0.1909 0.170

Elb/hr 2.05E-01 1.61E-01 2.13E-01 0.193

lb/mmBtuO2 3.53E-05 2.82E-05 3.91E-05 0.000

ug/dscm 4.52E+01 3.64E+01 4.95E+01 43.700

Location: Unit 1 - Method 5/OTM-28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 121.6 196.9 179.1 165.867

Elb/hr 1.41E+02 2.30E+02 2.08E+02 193.000

gr/dscf 1.39E-02 2.32E-02 2.06E-02 0.019

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 10.5 3.5 3.3 5.767

Elb/hr 1.22E+01 4.09E+00 3.84E+00 6.710

gr/dscf 1.20E-03 4.12E-04 3.80E-04 0.001

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 3.6 3.6 4.9 4.033

Elb/hr 4.19E+00 4.20E+00 5.70E+00 4.697

gr/dscf 4.12E-04 4.24E-04 5.64E-04 0.000

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 133.7 205 185.4 174.700

Elb/hr 1.56E+02 2.39E+02 2.16E+02 203.667

gr/dscf 1.53E-02 2.41E-02 2.13E-02 0.020

Location: Unit 1 - Method 6C

Compound: Sulfur Dioxide

Average

Saturday, January 15, 2011 Page 10 of 21
Hatfield Ferry Power Station

8/6/2010

Process Run Data

Run 1 2 3

ppm 1.67E+01 1.56E+01 1.28E+01 15.033

ppm@7%O2 1.43E+01 1.34E+01 1.10E+01 12.900

Location: Unit 1 - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

ppm 3.60E+02 3.73E+02 3.73E+02 368.667

ppm@7%O2 3.07E+02 3.20E+02 3.20E+02 315.667

Saturday, January 15, 2011 Page 11 of 21
Hatfield Ferry Power Station

8/6/2010

Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input 0 Million Btus/hr

Run Name Value UOM Comments

Target

Value

1 ELECTROSTATIC PRECIPITATOR 0 0

1 WET SCRUBBER 0 0

Run Name Value UOM Comments

1 Hydrogen 4.81 %

2 Hydrogen 4.81 %

3 Hydrogen 4.89 %

4 Hydrogen 0 %

1 Carbon 72.53 %

2 Carbon 73.14 %

3 Carbon 72.51 %

4 Carbon 0 %

1 Nitrogen 1.41 %

2 Nitrogen 1.43 %

3 Nitrogen 1.42 %

4 Nitrogen 0 %

1 Sulfur 1.95 %

2 Sulfur 2.13 %

3 Sulfur 2.21 %

4 Sulfur 0 %

1 Oxygen 7.14 %

2 Oxygen 6.78 %

3 Oxygen 6.96 %

4 Oxygen 0 %

1 Ash 12.16 %

2 Ash 11.71 %

3 Ash 12.01 %

4 Ash 0 %

1 Moisture Content 2.33 %

2 Moisture Content 2.08 %

3 Moisture Content 2.25 %

4 Moisture Content 0 %

1 Higher Heating Value, dry basis 12919 BTU/hr

Saturday, January 15, 2011 Page 12 of 21
Hatfield Ferry Power Station

8/6/2010

2 Higher Heating Value, dry basis 13094 BTU/hr

3 Higher Heating Value, dry basis 12986 BTU/hr

4 Higher Heating Value, dry basis 0 BTU/hr

Saturday, January 15, 2011 Page 13 of 21
Hatfield Ferry Power Station

8/6/2010

Sampling / Stack Data Results Detail

Location Unit 1 - Method 0011

Average

Run Number 1 2 3

Test Date 5/12/2010 5/12/2010 5/12/2010

Run Start Time 7:10:00 AM 10:00:00 AM 12:35:00 PM

Run Finish Time 9:21:00 AM 12:16:00 PM 2:52:00 PM

Net Traversing Points 24 24 24

Net Run Time, minutes 120 120 120

Nozzle Diameter, inches 0.22 0.22 0.22 0.220

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.998 0.998 0.998 0.998

Barometric Pressure, inches of Mercury 29.22 29.22 29.22 29.220

Average Orifice Meter Differential, inches H2O 1.27 1.36 1.36 1.330

Dry Gas Meter Volume Sampled, cubic feet 77.350 80.920 80.190 79.487

Average Dry Gas Meter Temperature, °F 93.35 97.10 98.79 96.413

Dry Gas Meter Volume Sampled, dscf 72.165 75.005 74.103 73.758

Total Moisture Liquid collected, g 272.4 264.4 292.2 276.333

Volume of Water Vapor, standard cubic feet 12.82 12.45 13.75 13.007

Moisture Content of Stack Gas, % 15.09 14.24 15.65 14.993

Moisture Saturation at Stack Gas Temperature, % 14.93 15.11 15.74 15.260

Dry Mole Fraction 0.8507 0.8576 0.8435 0.851

Carbon Dioxide, % 14.81 14.73 14.58 14.707

Oxygen, % 4.62 4.7 4.72 4.680

Carbon Monoxide & Nitrogen, % 80.57 80.57 80.7 80.613

Fuel Factor 1.10 1.10 1.11

Dry Molecular Weight, lb/lb-Mole 30.55 30.54 30.52 30.537

Wet Molecular weight, lb/lb-Mole 28.71 28.75 28.56 28.673

Flue Gas Static Pressure, inches of H2O -0.5 -0.5 -0.5 -0.500

Absolute Flue Gas Pressure, inches of Mercury 29.18 29.18 29.18 29.180

Average Stack Gas Temperature, °F 128.63 129.08 130.63 129.447

Average Velocity Head, inches of H2O 0.7072817906

3469

0.757539759

028044

0.767614217

280742

0.744

Average Stack Gas Velocity, feet/second 50.62 52.37 52.97 51.987

Stack Cross-Sectional Area, square feet 530.929 530.929 530.929 530.929

Dry Volumetric Flow Rate, dry scfm 1,200,056.0 1,250,657.5 1,240,923.1 1,230,545.5

33

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,612,537.6 1,668,285.1 1,687,398.5 1,656,073.7

33

Percent Isokinetic of Sampling Rate, % 100.8 100.5 100.1 100.467

Percent Excess Air, % 27.7 28.4 28.5 28.200

F-Factor, dscfm/MMBtu @ %O2 9796 9837 9720 9,784.333

Round Duct Diameter, inches 312 312 312

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

Saturday, January 15, 2011 Page 14 of 21
Hatfield Ferry Power Station

8/6/2010

Location Unit 1 - 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

Saturday, January 15, 2011 Page 15 of 21
Hatfield Ferry Power Station

8/6/2010

Location Unit 1 - 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

Saturday, January 15, 2011 Page 16 of 21
Hatfield Ferry Power Station

8/6/2010

Location Unit 1 - 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

Saturday, January 15, 2011 Page 17 of 21
Hatfield Ferry Power Station

8/6/2010

Location Unit 1 - 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

Saturday, January 15, 2011 Page 18 of 21
Hatfield Ferry Power Station

8/6/2010

Location Unit 1 - Method 5/OTM-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

Saturday, January 15, 2011 Page 19 of 21
Hatfield Ferry Power Station

8/6/2010

Location Unit 1 - 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

Saturday, January 15, 2011 Page 20 of 21
Hatfield Ferry Power Station

8/6/2010

Location Unit 1 - 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

Saturday, January 15, 2011 Page 21 of 21