Name:

Title:

Company:

Sign Date:

Name:

Title:

Company:

Sign Date:

Permitted Facility Representative / Date Testing Company Representative / Date

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.

Friday, January 14, 2011 Page 1 of 33
Facility Information:

AES Hawaii, INC

91-086 Kaomi Loop

Kapolei HI 96707

Contact: Sabrina Guanio

Phone: (808) 682-3412

Fax:

Email: Sabrina.Guanio@aes.com

Testing Company:

URS Corporation

1600 Perimeter Park

Suite 400

Morrisville NC 27560

Contact:Brad Justus

Phone: 919-461-1326

Fax: 919-461-1415

Email: Brad_Justus@urscorp.com

Air Permit Number:

10673

Permitted Source ID/Name:

BLRA BLRA

Permitted Maximum Process Rate:

N/A

Max. Normal Operation Process Rate:

N/A

Target Process Test Rate

N/A

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

 process flow diagram:

198 MW, circulating fluidized bed combustor, selective non-catalytic reduction, and a baghouse

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: FRS #: 110037260923

SCC / Description 10100218 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Atmospheric Fluidized Bed Combustion: Circulating Bed (Bitum. 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 0 127.5 109 0 235 59 6 5

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

Friday, January 14, 2011 Page 2 of 33
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

Stack Exit Hydrogen Chloride Method 26A 3 180 0

Stack Exit Hydrogen Fluoride Method 26A 3 180 0

Inorganic (Aqueous) 

Condensible Part.

OTM - 27/28 3 375 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Filterable PM2.5 OTM - 27/28 3 375 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Organic Condensible 

Particulate

OTM - 27/28 3 375 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Friday, January 14, 2011 Page 3 of 33
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.

Total PM2.5 OTM - 27/28 3 375 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Total Particulate OTM - 27/28 3 375 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Filterable Particulate OTM - 27/28 3 375 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Stack Exit Beryllium Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Mercury Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Selenium Method 29 3 240 0

Stack Exit Lead Method 29 3 240 0

Stack Exit Chromium Method 29 3 240 0

Stack Exit Magnesium Method 29 3 240 0

Stack Exit Cadmium Method 29 3 240 0

Stack Exit Filterable Particulate Method 29 3 240 0

Stack Exit Arsenic Method 29 3 240 0

Stack Exit Cobalt Method 29 3 240 0

Stack Exit Antimony Method 29 3 240 0

Stack Exit Co2 Method 3A CO2 3 120 0

Stack Exit O2 Method 3A O2 3 240 0

Stack Exit O2 Method 3A O2 3 120 0

Stack Exit O2 Method 3A O2 3 480 0

Stack Exit Co2 Method 3A CO2 3 480 0

Stack Exit Co2 Method 3A CO2 3 240 0

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

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

Friday, January 14, 2011 Page 4 of 33
Sampling / Stack Data Results Summary

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

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

Friday, January 14, 2011 Page 5 of 33
Location Stack Exit - Method 26A

Average

Run Number 1 2 3

Test Date 4/5/2010 4/6/2010 4/7/2010

Run Start Time 2:03:00 PM 7:25:00 

AM

2:06:00 PM

Run Finish Time 5:10:00 PM 10:30:00 

AM

5:11:00 PM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 129.193 122.721 125.634 125.849

Moisture Content of Stack Gas, % 9.36 9.63 9.74 9.577

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

Carbon Dioxide, % 14.3 14.3 14.2 14.267

Oxygen, % 5.4 5.4 5.5 5.433

Average Stack Gas Temperature, °F 299.13 296.67 300.37 298.723

Dry Volumetric Flow Rate, dry scfm 232,722.3 227,885.0 234,540.6 231,715.967

Actual Wet Volumetric Flue Gas Flow Rate, acfm 384,437.9 377,662.9 388,491.4 383,530.733

Percent Isokinetic of Sampling Rate, % 106.5 103.3 102.8 104.200

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 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

Friday, January 14, 2011 Page 6 of 33
Location Stack Exit - Method 3A CO2

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 3A CO2 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

Friday, January 14, 2011 Page 7 of 33
Location Stack Exit - Method 3A CO2 3 6

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack Exit - Method 3A O2

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

Friday, January 14, 2011 Page 8 of 33
Location Stack Exit - Method 3A O2 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 3A O2 3 6

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Friday, January 14, 2011 Page 9 of 33
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

Friday, January 14, 2011 Page 10 of 33
Emissions Summary

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

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

gr/dscf 1.83E-02 1.59E-02 1.60E-02 0.017

lb/mmBtuO2 3.41E-02 2.97E-02 2.98E-02 0.031

mg/dscm 4.18E+01 3.63E+01 3.66E+01 38.233

ppm 3.59E+01 3.12E+01 3.15E+01 32.867

ppm@7%O2 3.19E+01 2.78E+01 2.79E+01 29.200

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 2.42E-04 2.46E-04 2.33E-04 0.000

lb/mmBtuO2 4.51E-04 4.59E-04 4.33E-04 0.000

mg/dscm 5.53E-01 5.62E-01 5.32E-01 0.549

ppm 3.02E-01 3.07E-01 2.90E-01 0.300

ppm@7%O2 2.68E-01 2.73E-01 2.57E-01 0.266

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 13.37 12.355 11.801 12.509

Elb/hr 3.19E+00 3.03E+00 2.91E+00 3.043

lb/mmBtuO2 3.01E-03 2.93E-03 2.75E-03 0.003

mg/dscm 3.66E+00 3.56E+00 3.32E+00 3.513

mg/dscm@7%O2 3.28E+00 3.19E+00 3.00E+00 3.157

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.279 0.26 0.266 0.268

Elb/hr 6.65E-02 6.39E-02 6.57E-02 0.065

lb/mmBtuO2 6.28E-05 6.16E-05 6.20E-05 0.000

mg/dscm 7.63E-02 7.48E-02 7.48E-02 0.075

mg/dscm@7%O2 6.84E-02 6.71E-02 6.75E-02 0.068

Location: Stack Exit - Method 29 

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.0000054 0.0000354 0.000055 0.000

Elb/hr 9.76E-07 6.49E-06 1.03E-05 0.000

lb/mmBtuO2 9.35E-10 6.12E-09 9.82E-09 0.000

mg/dscm 1.14E-06 7.43E-06 1.19E-05 0.000

mg/dscm@7%O2 1.02E-06 6.66E-06 1.07E-05 0.000

Friday, January 14, 2011 Page 11 of 33
Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.00015 0.00015 0.00015 0.000

Elb/hr 2.71E-05 2.75E-05 2.81E-05 0.000

lb/mmBtuO2 2.60E-08 2.59E-08 2.68E-08 0.000

mg/dscm 3.15E-05 3.15E-05 3.25E-05 0.000

mg/dscm@7%O2 2.82E-05 2.82E-05 2.91E-05 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.000024 0.000024 0.000024 0.000

Elb/hr 4.34E-06 4.40E-06 4.50E-06 0.000

lb/mmBtuO2 4.15E-09 4.15E-09 4.29E-09 0.000

mg/dscm 5.05E-06 5.04E-06 5.21E-06 0.000

mg/dscm@7%O2 4.53E-06 4.52E-06 4.67E-06 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.000086 0.000122 0.000069 0.000

Elb/hr 1.55E-05 2.24E-05 1.29E-05 0.000

lb/mmBtuO2 1.49E-08 2.11E-08 1.23E-08 0.000

mg/dscm 1.81E-05 2.56E-05 1.50E-05 0.000

mg/dscm@7%O2 1.62E-05 2.30E-05 1.35E-05 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.19867 0.00469 0.00207 0.068

Elb/hr 3.59E-02 8.59E-04 3.88E-04 0.012

lb/mmBtuO2 3.44E-05 8.11E-07 3.70E-07 0.000

mg/dscm 4.18E-02 9.85E-04 4.49E-04 0.014

mg/dscm@7%O2 3.75E-02 8.83E-04 4.03E-04 0.013

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.000909 0.000249 0.000123 0.000

Elb/hr 1.64E-04 4.56E-05 2.31E-05 0.000

lb/mmBtuO2 1.57E-07 4.30E-08 2.20E-08 0.000

mg/dscm 1.91E-04 5.23E-05 2.67E-05 0.000

mg/dscm@7%O2 1.71E-04 4.69E-05 2.39E-05 0.000

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 11 4.4 3.2 6.200

Elb/hr 1.99E+00 8.06E-01 6.00E-01 1.132

lb/mmBtuO2 1.90E-03 7.61E-04 5.71E-04 0.001

mg/dscm 2.31E+00 9.24E-01 6.94E-01 1.309

mg/dscm@7%O2 2.07E+00 8.29E-01 6.22E-01 1.174

Friday, January 14, 2011 Page 12 of 33
Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.00058 0.00225 0.00162 0.001

Elb/hr 1.05E-04 4.12E-04 3.04E-04 0.000

lb/mmBtuO2 1.00E-07 3.89E-07 2.89E-07 0.000

mg/dscm 1.22E-04 4.73E-04 3.51E-04 0.000

mg/dscm@7%O2 1.09E-04 4.24E-04 3.15E-04 0.000

Compound: Magnesium

Average

RunNumber 1 2 3

Mass_mg 0 0 0 0.000

Elb/hr 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

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

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.008821 0.002031 0.000871 0.004

Elb/hr 1.59E-03 3.72E-04 1.63E-04 0.001

lb/mmBtuO2 1.53E-06 3.51E-07 1.56E-07 0.000

mg/dscm 1.86E-03 4.27E-04 1.89E-04 0.001

mg/dscm@7%O2 1.67E-03 3.83E-04 1.69E-04 0.001

Compound: Mercury

Average

RunNumber 1 2 3

Mass_mg 0 0 0 0.000

Elb/hr 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

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

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.033693 0.006713 0.004633 0.015

Elb/hr 6.09E-03 1.23E-03 8.68E-04 0.003

lb/mmBtuO2 5.83E-06 1.16E-06 8.27E-07 0.000

mg/dscm 7.09E-03 1.41E-03 1.01E-03 0.003

mg/dscm@7%O2 6.36E-03 1.26E-03 9.06E-04 0.003

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.00026 0.00032 0.00033 0.000

Elb/hr 4.70E-05 5.86E-05 6.19E-05 0.000

lb/mmBtuO2 4.50E-08 5.53E-08 5.89E-08 0.000

mg/dscm 5.47E-05 6.72E-05 7.16E-05 0.000

mg/dscm@7%O2 4.91E-05 6.03E-05 6.42E-05 0.000

Friday, January 14, 2011 Page 13 of 33
Process Run Data

Location: Stack Exit - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 2.5 7.7 2.1 4.100

lb/mmBtuO2 5.38E-04 1.70E-03 4.60E-04 0.001

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 1.1 3.4 1 1.833

lb/mmBtuO2 2.37E-04 7.51E-04 2.19E-04 0.000

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 17.1 18.6 17.3 17.667

lb/mmBtuO2 3.68E-03 4.11E-03 3.79E-03 0.004

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 4.4 3.5 3.8 3.900

lb/mmBtuO2 9.47E-04 7.73E-04 8.33E-04 0.001

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 24 29.8 23.2 25.667

lb/mmBtuO2 5.17E-03 6.58E-03 5.08E-03 0.006

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 22.6 25.5 22.1 23.400

lb/mmBtuO2 4.86E-03 5.63E-03 4.84E-03 0.005

Friday, January 14, 2011 Page 14 of 33
Process Run Data

Run Name Value UOM Comments

Target

Value

1 Bituminous Coal Burned 1087.3 Tons/hr 0

2 Bituminous Coal Burned 1089.6 Tons/hr 0

3 Bituminous Coal Burned 1095.4 Tons/hr 0

4 Bituminous Coal Burned 1079.8 Tons/hr 0

5 Bituminous Coal Burned 1093.6 Tons/hr 0

6 Bituminous Coal Burned 1095.3 Tons/hr 0

7 Bituminous Coal Burned 1079.8 Tons/hr 0

8 Bituminous Coal Burned 1081.1 Tons/hr 0

9 Bituminous Coal Burned 1080.6 Tons/hr 0

1 Average Heat Input 0 MMBtu/hr 0

2 Average Heat Input 0 MMBtu/hr 0

3 Average Heat Input 0 MMBtu/hr 0

4 Average Heat Input 0 MMBtu/hr 0

5 Average Heat Input 0 MMBtu/hr 0

6 Average Heat Input 0 MMBtu/hr 0

7 Average Heat Input 0 MMBtu/hr 0

8 Average Heat Input 0 MMBtu/hr 0

9 Average Heat Input 0 MMBtu/hr 0

1 Steam Output 669 1000 lb steam/hr 0

2 Steam Output 663.71 1000 lb steam/hr 0

3 Steam Output 666.76 1000 lb steam/hr 0

4 Steam Output 662.98 1000 lb steam/hr 0

5 Steam Output 667.07 1000 lb steam/hr 0

6 Steam Output 667.08 1000 lb steam/hr 0

7 Steam Output 671.3 1000 lb steam/hr 0

8 Steam Output 678.35 1000 lb steam/hr 0

9 Steam Output 679.47 1000 lb steam/hr 0

1 Synfuel Firing Rate 0 0

2 Synfuel Firing Rate 0 0

3 Synfuel Firing Rate 0 0

4 Synfuel Firing Rate 0 0

5 Synfuel Firing Rate 0 0

6 Synfuel Firing Rate 0 0

Friday, January 14, 2011 Page 15 of 33
7 Synfuel Firing Rate 0 0

8 Synfuel Firing Rate 0 0

9 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

4 Petroleum Coke Firing Rate 0 0

5 Petroleum Coke Firing Rate 0 0

6 Petroleum Coke Firing Rate 0 0

7 Petroleum Coke Firing Rate 0 0

8 Petroleum Coke Firing Rate 0 0

9 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

4 Coal Gas Firing Rate 0 0

5 Coal Gas Firing Rate 0 0

6 Coal Gas Firing Rate 0 0

7 Coal Gas Firing Rate 0 0

8 Coal Gas Firing Rate 0 0

9 Coal Gas Firing Rate 0 0

1 Fuel Oil Firing Rate 0 0

2 Fuel Oil Firing Rate 0 0

3 Fuel Oil Firing Rate 0 0

4 Fuel Oil Firing Rate 0 0

5 Fuel Oil Firing Rate 0 0

6 Fuel Oil Firing Rate 0 0

7 Fuel Oil Firing Rate 0 0

8 Fuel Oil Firing Rate 0 0

9 Fuel Oil Firing Rate 0 0

1 Flue Gas Flow Rate 0 dscfm 0

4 Flue Gas Flow Rate 0 dscfm 0

5 Flue Gas Flow Rate 0 dscfm 0

6 Flue Gas Flow Rate 0 dscfm 0

7 Flue Gas Flow Rate 0 dscfm 0

8 Flue Gas Flow Rate 0 dscfm 0

Friday, January 14, 2011 Page 16 of 33
9 Flue Gas Flow Rate 0 dscfm 0

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

4 Pressure Drop Across FGD (if applicable) 0 in H20 0

5 Pressure Drop Across FGD (if applicable) 0 in H20 0

6 Pressure Drop Across FGD (if applicable) 0 in H20 0

7 Pressure Drop Across FGD (if applicable) 0 in H20 0

8 Pressure Drop Across FGD (if applicable) 0 in H20 0

9 Pressure Drop Across FGD (if applicable) 0 in H20 0

1 FGD Scrubber Liquor pH 0 pH 0

4 FGD Scrubber Liquor pH 0 pH 0

5 FGD Scrubber Liquor pH 0 pH 0

6 FGD Scrubber Liquor pH 0 pH 0

7 FGD Scrubber Liquor pH 0 pH 0

8 FGD Scrubber Liquor pH 0 pH 0

9 FGD Scrubber Liquor pH 0 pH 0

1 FGD Scrubber Liquor Flow Rate 0 gal/min 0

4 FGD Scrubber Liquor Flow Rate 0 gal/min 0

5 FGD Scrubber Liquor Flow Rate 0 gal/min 0

6 FGD Scrubber Liquor Flow Rate 0 gal/min 0

7 FGD Scrubber Liquor Flow Rate 0 gal/min 0

8 FGD Scrubber Liquor Flow Rate 0 gal/min 0

9 FGD Scrubber Liquor Flow Rate 0 gal/min 0

1 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

4 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

5 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

6 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

7 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

8 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

9 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

1 Flue Gas Oxygen Content 0 % 0

4 Flue Gas Oxygen Content 0 % 0

5 Flue Gas Oxygen Content 0 % 0

Friday, January 14, 2011 Page 17 of 33
6 Flue Gas Oxygen Content 0 % 0

7 Flue Gas Oxygen Content 0 % 0

8 Flue Gas Oxygen Content 0 % 0

9 Flue Gas Oxygen Content 0 % 0

1 Flue Gas Carbon Dioxide Content 0 % 0

4 Flue Gas Carbon Dioxide Content 0 % 0

5 Flue Gas Carbon Dioxide Content 0 % 0

6 Flue Gas Carbon Dioxide Content 0 % 0

7 Flue Gas Carbon Dioxide Content 0 % 0

8 Flue Gas Carbon Dioxide Content 0 % 0

9 Flue Gas Carbon Dioxide Content 0 % 0

1 Flue Gas Moisture Content 0 % 0

4 Flue Gas Moisture Content 0 % 0

5 Flue Gas Moisture Content 0 % 0

6 Flue Gas Moisture Content 0 % 0

7 Flue Gas Moisture Content 0 % 0

8 Flue Gas Moisture Content 0 % 0

9 Flue Gas Moisture Content 0 % 0

1 Flue Gas Sampling Point Temperature 0 Deg F 0

4 Flue Gas Sampling Point Temperature 0 Deg F 0

5 Flue Gas Sampling Point Temperature 0 Deg F 0

6 Flue Gas Sampling Point Temperature 0 Deg F 0

7 Flue Gas Sampling Point Temperature 0 Deg F 0

8 Flue Gas Sampling Point Temperature 0 Deg F 0

9 Flue Gas Sampling Point Temperature 0 Deg F 0

1 Flue Gas Pressure 0 atm 0

4 Flue Gas Pressure 0 atm 0

5 Flue Gas Pressure 0 atm 0

6 Flue Gas Pressure 0 atm 0

7 Flue Gas Pressure 0 atm 0

8 Flue Gas Pressure 0 atm 0

9 Flue Gas Pressure 0 atm 0

1 Standard Pressure 0 atm 0

4 Standard Pressure 0 atm 0

5 Standard Pressure 0 atm 0

6 Standard Pressure 0 atm 0

Friday, January 14, 2011 Page 18 of 33
APCD Run Data

Process Lab Run Data

7 Standard Pressure 0 atm 0

8 Standard Pressure 0 atm 0

9 Standard Pressure 0 atm 0

1 Standard Temperature 0 Deg F 0

4 Standard Temperature 0 Deg F 0

5 Standard Temperature 0 Deg F 0

6 Standard Temperature 0 Deg F 0

7 Standard Temperature 0 Deg F 0

8 Standard Temperature 0 Deg F 0

9 Standard Temperature 0 Deg F 0

1 Unit Gross Electrical Output 197.1 MW 0

4 Unit Gross Electrical Output 197.37 MW 0

5 Unit Gross Electrical Output 196.69 MW 0

6 Unit Gross Electrical Output 197.07 MW 0

7 Unit Gross Electrical Output 196.96 MW 0

8 Unit Gross Electrical Output 196.89 MW 0

9 Unit Gross Electrical Output 196.76 MW 0

1 Unit Net Electric Generation 0 MWh 0

4 Unit Net Electric Generation 0 MWh 0

5 Unit Net Electric Generation 0 MWh 0

6 Unit Net Electric Generation 0 MWh 0

7 Unit Net Electric Generation 0 MWh 0

8 Unit Net Electric Generation 0 MWh 0

9 Unit Net Electric Generation 0 MWh 0

Run Name Value UOM Comments

Target

Value

1 SELECTIVE NONCATALYTIC REDUCTION 

FOR NOX

0 0

1 BAGHOUSE 0 0

1 desription in section 5a. 0 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value 12179 Btu/lb

2 Fuel Higher Heating Value 11962 Btu/lb

Friday, January 14, 2011 Page 19 of 33
3 Fuel Higher Heating Value 12096 Btu/lb 4 Fuel Higher Heating Value 11905 Btu/lb 5 Fuel Higher Heating Value 12032 Btu/lb 6 Fuel Higher Heating Value 12231 Btu/lb 7 Fuel Higher Heating Value 11863 Btu/lb 8 Fuel Higher Heating Value 11812 Btu/lb 9 Fuel Higher Heating Value 11795 Btu/lb 1 Fuel Moisture 14 % 2 Fuel Moisture 14 % 3 Fuel Moisture 15 % 4 Fuel Moisture 15 % 5 Fuel Moisture 17 % 6 Fuel Moisture 16 % 7 Fuel Moisture 16 % 8 Fuel Moisture 16 % 9 Fuel Moisture 17 % 1 Fuel Mercury Content 0.040 ppm 2 Fuel Mercury Content 0.055 ppm 3 Fuel Mercury Content 0.067 ppm 4 Fuel Mercury Content 0.044 ppm 5 Fuel Mercury Content 0.075 ppm 6 Fuel Mercury Content 0.055 ppm 7 Fuel Mercury Content 0 ppm 8 Fuel Mercury Content 0 ppm 9 Fuel Mercury Content 0 ppm 1 Fuel Cadmium Content 0 ppm 2 Fuel Cadmium Content 0 ppm 3 Fuel Cadmium Content 0 ppm 4 Fuel Cadmium Content 0 ppm 5 Fuel Cadmium Content 0.49 ppm 6 Fuel Cadmium Content 0 ppm 7 Fuel Cadmium Content 0 ppm 8 Fuel Cadmium Content 0 ppm 9 Fuel Cadmium Content 0 ppm 1 Ultimate/Proximate Analysis 0 2 Ultimate/Proximate Analysis 0 3 Ultimate/Proximate Analysis 0 4 Ultimate/Proximate Analysis 0 5 Ultimate/Proximate Analysis 0 6 Ultimate/Proximate Analysis 0 7 Ultimate/Proximate Analysis 0 8 Ultimate/Proximate Analysis 0 9 Ultimate/Proximate Analysis 0

Friday, January 14, 2011 Page 20 of 33
1 Fuel Nickel Content 7.9 ppm 2 Fuel Nickel Content 8.1 ppm 3 Fuel Nickel Content 7.4 ppm 4 Fuel Nickel Content 7.7 ppm 5 Fuel Nickel Content 11 ppm 6 Fuel Nickel Content 7.6 ppm 7 Fuel Nickel Content 0 ppm 8 Fuel Nickel Content 0 ppm 9 Fuel Nickel Content 0 ppm 1 Fuel Arsenic Content 2.1 ppm 2 Fuel Arsenic Content 1.4 ppm 3 Fuel Arsenic Content 1.6 ppm 4 Fuel Arsenic Content 1.6 ppm 5 Fuel Arsenic Content 1.7 ppm 6 Fuel Arsenic Content 1.7 ppm 7 Fuel Arsenic Content 0 ppm 8 Fuel Arsenic Content 0 ppm 9 Fuel Arsenic Content 0 ppm 1 Fuel Chromium Content 5.3 ppm 2 Fuel Chromium Content 6.9 ppm 3 Fuel Chromium Content 5.7 ppm 4 Fuel Chromium Content 5.3 ppm 5 Fuel Chromium Content 7 ppm 6 Fuel Chromium Content 5.6 ppm 7 Fuel Chromium Content 0 ppm 8 Fuel Chromium Content 0 ppm 9 Fuel Chromium Content 0 ppm 1 Fuel Beryllium Content 0.44 ppm 2 Fuel Beryllium Content 0.6 ppm 3 Fuel Beryllium Content 0.6 ppm 4 Fuel Beryllium Content 0.4 ppm 5 Fuel Beryllium Content 0.7 ppm 6 Fuel Beryllium Content 0.6 ppm 7 Fuel Beryllium Content 0 ppm 8 Fuel Beryllium Content 0 ppm 9 Fuel Beryllium Content 0 ppm 1 Fuel Lead Content 3.8 ppm 2 Fuel Lead Content 4.3 ppm 3 Fuel Lead Content 3.9 ppm 4 Fuel Lead Content 4.3 ppm 5 Fuel Lead Content 11 ppm 6 Fuel Lead Content 4.5 ppm 7 Fuel Lead Content 0 ppm

Friday, January 14, 2011 Page 21 of 33
8 Fuel Lead Content 0 ppm

9 Fuel Lead Content 0 ppm

1 Fuel Manganese Content 39 ppm

2 Fuel Manganese Content 45 ppm

3 Fuel Manganese Content 57 ppm

4 Fuel Manganese Content 37 ppm

5 Fuel Manganese Content 149 ppm

6 Fuel Manganese Content 44 ppm

7 Fuel Manganese Content 0 ppm

8 Fuel Manganese Content 0 ppm

9 Fuel Manganese Content 0 ppm

1 Fuel Chlorine Content 74 ppm

2 Fuel Chlorine Content 74 ppm

3 Fuel Chlorine Content 68 ppm

4 Fuel Chlorine Content 63 ppm

5 Fuel Chlorine Content 67 ppm

6 Fuel Chlorine Content 63 ppm

7 Fuel Chlorine Content 63 ppm

8 Fuel Chlorine Content 62 ppm

9 Fuel Chlorine Content 61 ppm

1 Fuel Fluorine Content 0 ppm

2 Fuel Fluorine Content 0 ppm

3 Fuel Fluorine Content 0 ppm

4 Fuel Fluorine Content 0 ppm

5 Fuel Fluorine Content 0 ppm

6 Fuel Fluorine Content 0 ppm

7 Fuel Fluorine Content 56 ppm

8 Fuel Fluorine Content 67 ppm

9 Fuel Fluorine Content 61 ppm

Friday, January 14, 2011 Page 22 of 33
Sampling / Stack Data Results Detail

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

Friday, January 14, 2011 Page 23 of 33
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

Friday, January 14, 2011 Page 24 of 33
Location Stack Exit - Method 26A

Average

Run Number 1 2 3

Test Date 4/5/2010 4/6/2010 4/7/2010

Run Start Time 2:03:00 PM 7:25:00 AM 2:06:00 PM

Run Finish Time 5:10:00 PM 10:30:00 AM 5:11:00 PM

Net Traversing Points 31 31 31

Net Run Time, minutes 180 180 180

Nozzle Diameter, inches 0.226333333 0.226333333 0.226333333 0.226

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.994 0.994 0.994 0.994

Barometric Pressure, inches of Mercury 30.27 30.25 30.25 30.257

Average Orifice Meter Differential, inches H2O 1.50 0.93 0.98 1.137

Dry Gas Meter Volume Sampled, cubic feet 131.162 125.543 128.626 128.444

Average Dry Gas Meter Temperature, °F 81.03 84.05 84.55 83.210

Dry Gas Meter Volume Sampled, dscf 129.193 122.721 125.634 125.849

Total Moisture Liquid collected, g 283.4 277.8 287.8 283.000

Volume of Water Vapor, standard cubic feet 13.34 13.08 13.55 13.323

Moisture Content of Stack Gas, % 9.36 9.63 9.74 9.577

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

Dry Mole Fraction 0.9064 0.9037 0.9026 0.904

Carbon Dioxide, % 14.3 14.3 14.2 14.267

Oxygen, % 5.4 5.4 5.5 5.433

Carbon Monoxide & Nitrogen, % 80.3 80.3 80.3 80.300

Fuel Factor 1.08 1.08 1.08

Dry Molecular Weight, lb/lb-Mole 30.50 30.50 30.49 30.497

Wet Molecular weight, lb/lb-Mole 29.33 29.30 29.27 29.300

Flue Gas Static Pressure, inches of H2O -21 -22 -19.5 -20.833

Absolute Flue Gas Pressure, inches of Mercury 28.73 28.63 28.82 28.727

Average Stack Gas Temperature, °F 299.13 296.67 300.37 298.723

Average Velocity Head, inches of H2O 0.9488209474

22606

0.914494742

728271

0.968222668

83143

0.944

Average Stack Gas Velocity, feet/second 66.39 65.22 67.09 66.233

Stack Cross-Sectional Area, square feet 96.510 96.510 96.510 96.510

Dry Volumetric Flow Rate, dry scfm 232,722.3 227,885.0 234,540.6 231,715.967

Actual Wet Volumetric Flue Gas Flow Rate, acfm 384,437.9 377,662.9 388,491.4 383,530.733

Percent Isokinetic of Sampling Rate, % 106.5 103.3 102.8 104.200

Percent Excess Air, % 34.2 34.2 35.0 34.467

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

Round Duct Diameter, inches 0 0 0

Rectangular Duct Width, inches 109 109 109

Rectangular Duct Length, inches 127.5 127.5 127.5

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Friday, January 14, 2011 Page 25 of 33
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

Friday, January 14, 2011 Page 26 of 33
Location Stack Exit - Method 3A CO2

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

Friday, January 14, 2011 Page 27 of 33
Location Stack Exit - Method 3A CO2 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

Friday, January 14, 2011 Page 28 of 33
Location Stack Exit - Method 3A CO2 3 6

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Friday, January 14, 2011 Page 29 of 33
Location Stack Exit - Method 3A O2

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

Friday, January 14, 2011 Page 30 of 33
Location Stack Exit - Method 3A O2 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

Friday, January 14, 2011 Page 31 of 33
Location Stack Exit - Method 3A O2 3 6

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Friday, January 14, 2011 Page 32 of 33
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

Friday, January 14, 2011 Page 33 of 33