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.

Wednesday, February 02, 2011 Page 1 of 32
Facility Information:

NC_Riverbend Unit 7A

175 Steam Plant Road

Mt. Holly NC 28120

Contact: Jon Hays

Phone: 317-838-4445

Fax: 317-8382490

Email: jon.hays@duke.energy.com

Testing Company:

AECOM

2 Technology Park Drive

Westford MA 01886

Contact: Patrick Ford

Phone: 978-589-3427

Fax: 978-589-3100

Email: pat.ford@aecom.com

Air Permit Number:

03788T31

Permitted Source ID/Name:

Unit 7A No. 2 Fuel Oil/Coal-Fired Electric Utility Boiler

Permitted Maximum Process Rate:

1058 MMBtu/hr

Max. Normal Operation Process Rate:

1058 MMBtu/hr

Target Process Test Rate

1058 MMBtu/hr

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

 process flow diagram:

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

similarity with others of same SCC.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 110000348641 FRS #: 3707100040

SCC / Description 10100201 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Pulverized Coal: Wet 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 102 0 0 0 8 2 4 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Exit Carbon Monoxide Method 10 3 60 0

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 4 120 0

Stack Exit Hydrogen Fluoride Method 26A 3 60 0

Stack Exit Hydrogen Chloride Method 26A 3 60 0

Organic Condensible 

Particulate

OTM - 27/28 3 345 0 R1-382 min, R2-340 

min, R3-314 min

Stack Exit

Wednesday, February 02, 2011 Page 2 of 32
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.

EPA Method 26A was modified to include the provisions cited in Method CTM-033 to allow simultaneous collection 

of HCl, HF and HCN. Modification included elimination of the 0.1 N H2SO4 impingers, addition of a third NaOH 

impinger and use of high normality NaOH absorbing solutions (6N in the 1st impinger and 2 N in the second and 

third) in order to maintain the pH of the solution high enough to prevent poor HCN analyte collection. The sample 

time was also reduced to 1-hour as allowed by EPA (see FAQ's section on the ICR website) again to ensure that the 

pH of the absorbing solution remained high.

Total PM2.5 OTM - 27/28 3 345 0 R1-382 min, R2-340 

min, R3-314 min

Stack Exit

Filterable PM2.5 OTM - 27/28 3 345 0 R1-382 min, R2-340 

min, R3-314 min

Stack Exit

Inorganic (Aqueous) 

Condensible Part.

OTM - 27/28 3 345 0 R1-382 min, R2-340 

min, R3-314 min

Stack Exit

Stack Exit Cobalt Method 29 3 180 0

Stack Exit Manganese Method 29 3 180 0

Stack Exit Lead Method 29 3 180 0

Stack Exit Antimony Method 29 3 180 0

Stack Exit Nickel Method 29 3 180 0

Stack Exit Arsenic Method 29 3 180 0

Stack Exit Chromium Method 29 3 180 0

Stack Exit Selenium Method 29 3 180 0

Stack Exit Cadmium Method 29 3 180 0

Stack Exit Filterable Particulate Method 29 3 180 0

Stack Exit Beryllium Method 29 3 180 0

Stack Exit O2 Method 3A O2 3 60 0

Stack Exit Co2 Method 3A CO2 3 60 0

Stack Exit Sulfur Dioxide Method 6C 3 60 0

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

Wednesday, February 02, 2011 Page 3 of 32
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 10 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Wednesday, February 02, 2011 Page 4 of 32
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 CTM033-

7A-1

CTM033-

7A-2

CTM033-

7A-3

Test Date 4/7/2010 4/7/2010 4/7/2010

Run Start Time 9:08:00 AM 10:42:00 

AM

12:25:00 PM

Run Finish Time 10:15:00 AM 11:51:00 

AM

1:31:00 PM

Net Run Time, minutes 60 60 60

Dry Gas Meter Volume Sampled, dscf 36.653 36.854 36.359 36.622

Moisture Content of Stack Gas, % 9.37 9.59 9.08 9.347

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

Carbon Dioxide, % 12.83 12.87 12.82 12.840

Oxygen, % 6.99 6.94 6.95 6.960

Average Stack Gas Temperature, °F 320.83 323.42 324.58 322.943

Dry Volumetric Flow Rate, dry scfm 124,870.2 125,228.7 124,835.7 124,978.200

Actual Wet Volumetric Flue Gas Flow Rate, acfm 208,708.1 210,512.6 208,912.4 209,377.700

Percent Isokinetic of Sampling Rate, % 103.3 103.5 102.5 103.100

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

Wednesday, February 02, 2011 Page 5 of 32
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 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

Wednesday, February 02, 2011 Page 6 of 32
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

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

Wednesday, February 02, 2011 Page 7 of 32
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

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

Wednesday, February 02, 2011 Page 8 of 32
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

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

Wednesday, February 02, 2011 Page 9 of 32
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

Wednesday, February 02, 2011 Page 10 of 32
Emissions Summary

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run CTM033-7A-1 CTM033-7A-2 CTM033-7A-3

Elb/hr 1.78E+01 2.41E+01 2.87E+01 23.533

lb/mmBtuO2 3.49E-02 4.70E-02 5.62E-02 0.046

ppm 3.27E+01 4.41E+01 5.28E+01 43.200

ppm@7%O2 3.27E+01 4.39E+01 5.26E+01 43.067

Location: Stack Exit - Method 10 3

Compound: Carbon Monoxide

Average

Run Organic-7A-1 Organic-7A-2 Organic-7A-3

Elb/hr 2.99E+01 2.90E+01 2.72E+01 28.700

lb/mmBtuO2 5.75E-02 5.44E-02 5.09E-02 0.054

ppm 5.41E+01 5.13E+01 4.79E+01 51.100

ppm@7%O2 5.38E+01 5.10E+01 4.76E+01 50.800

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 6.25E-04 3.38E-04 4.23E-04 0.000

ppm 3.73E-01 2.02E-01 2.53E-01 0.276

ppm@7%O2 3.71E-01 2.01E-01 2.52E-01 0.275

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber CTM033-7A-1 CTM033-7A-2 CTM033-7A-3

Mass_mg 81.134 82.195 82.658 81.996

Elb/hr 3.66E+01 3.69E+01 3.75E+01 37.000

lb/mmBtuO2 7.17E-02 7.20E-02 7.34E-02 0.072

mg/dscm 7.82E+01 7.88E+01 8.03E+01 79.100

mg/dscm@7%O2 7.81E+01 7.85E+01 8.00E+01 78.867

Compound: Hydrogen Fluoride

Average

RunNumber CTM033-7A-1 CTM033-7A-2 CTM033-7A-3

Mass_mg 8.29 8.57 8.35 8.403

Elb/hr 3.74E+00 3.85E+00 3.79E+00 3.793

lb/mmBtuO2 7.33E-03 7.51E-03 7.42E-03 0.007

mg/dscm 7.99E+00 8.21E+00 8.11E+00 8.103

mg/dscm@7%O2 7.98E+00 8.17E+00 8.08E+00 8.077

Location: Stack Exit - Method 29

Compound: Antimony

Average

RunNumber 7A-1 7A-2 7A-3

Wednesday, February 02, 2011 Page 11 of 32
Mass_mg 0.00092 0.00102 0.00513 0.002

Elb/hr 1.13E-04 1.21E-04 6.07E-04 0.000

gr/dscf 9.75E-08 1.07E-07 5.32E-07 0.000

gr/dscf@7%O2 9.67E-08 1.06E-07 5.29E-07 0.000

lb/mmBtuO2 2.03E-07 2.23E-07 1.11E-06 0.000

mg/dscm 2.23E-04 2.44E-04 1.22E-03 0.001

mg/dscm@7%O2 2.21E-04 2.42E-04 1.21E-03 0.001

ug/dscm 2.23E-01 2.44E-01 1.22E+00 0.562

ug/dscm@7%O2 2.21E-01 2.42E-01 1.21E+00 0.558

Compound: Arsenic

Average

RunNumber 7A-1 7A-2 7A-3

Mass_mg 0.05395 0.10755 0.16525 0.109

Elb/hr 6.60E-03 1.27E-02 1.95E-02 0.013

gr/dscf 5.72E-06 1.13E-05 1.71E-05 0.000

gr/dscf@7%O2 5.67E-06 1.12E-05 1.70E-05 0.000

lb/mmBtuO2 1.19E-05 2.35E-05 3.57E-05 0.000

mg/dscm 1.31E-02 2.58E-02 3.92E-02 0.026

mg/dscm@7%O2 1.30E-02 2.56E-02 3.89E-02 0.026

ug/dscm 1.31E+01 2.58E+01 3.92E+01 26.033

ug/dscm@7%O2 1.30E+01 2.56E+01 3.89E+01 25.833

Compound: Beryllium

Average

RunNumber 7A-1 7A-2 7A-3

Mass_mg 0.00092 0.00088 0.00761 0.003

Elb/hr 1.13E-04 1.04E-04 9.00E-04 0.000

gr/dscf 9.75E-08 9.21E-08 7.89E-07 0.000

gr/dscf@7%O2 9.67E-08 9.14E-08 7.84E-07 0.000

lb/mmBtuO2 2.03E-07 1.92E-07 1.65E-06 0.000

mg/dscm 2.23E-04 2.11E-04 1.80E-03 0.001

mg/dscm@7%O2 2.21E-04 2.09E-04 1.79E-03 0.001

ug/dscm 2.23E-01 2.11E-01 1.80E+00 0.745

ug/dscm@7%O2 2.21E-01 2.09E-01 1.79E+00 0.740

Compound: Cadmium

Average

RunNumber 7A-1 7A-2 7A-3

Mass_mg 0.0007 0.00039 0.00575 0.002

Elb/hr 8.56E-05 4.61E-05 6.80E-04 0.000

gr/dscf 7.42E-08 4.08E-08 5.96E-07 0.000

gr/dscf@7%O2 7.36E-08 4.05E-08 5.92E-07 0.000

lb/mmBtuO2 1.55E-07 8.51E-08 1.24E-06 0.000

mg/dscm 1.70E-04 9.34E-05 1.36E-03 0.001

mg/dscm@7%O2 1.69E-04 9.27E-05 1.35E-03 0.001

ug/dscm 1.70E-01 9.34E-02 1.36E+00 0.541

ug/dscm@7%O2 1.69E-01 9.27E-02 1.35E+00 0.537

Compound: Chromium

Average

RunNumber 7A-1 7A-2 7A-3

Mass_mg 0.0102 0.0094 0.0506 0.023

Elb/hr 1.25E-03 1.11E-03 5.99E-03 0.003

Wednesday, February 02, 2011 Page 12 of 32
gr/dscf 1.08E-06 9.84E-07 5.24E-06 0.000

gr/dscf@7%O2 1.07E-06 9.77E-07 5.21E-06 0.000

lb/mmBtuO2 2.25E-06 2.05E-06 1.09E-05 0.000

mg/dscm 2.47E-03 2.25E-03 1.20E-02 0.006

mg/dscm@7%O2 2.45E-03 2.23E-03 1.19E-02 0.006

ug/dscm 2.47E+00 2.25E+00 1.20E+01 5.573

ug/dscm@7%O2 2.45E+00 2.23E+00 1.19E+01 5.527

Compound: Cobalt

Average

RunNumber 7A-1 7A-2 7A-3

Mass_mg 0.004 0.0042 0.0308 0.013

Elb/hr 4.89E-04 4.96E-04 3.64E-03 0.002

gr/dscf 4.24E-07 4.40E-07 3.19E-06 0.000

gr/dscf@7%O2 4.20E-07 4.37E-07 3.17E-06 0.000

lb/mmBtuO2 8.83E-07 9.17E-07 6.66E-06 0.000

mg/dscm 9.70E-04 1.01E-03 7.30E-03 0.003

mg/dscm@7%O2 9.62E-04 1.00E-03 7.25E-03 0.003

ug/dscm 9.70E-01 1.01E+00 7.30E+00 3.093

ug/dscm@7%O2 9.62E-01 1.00E+00 7.25E+00 3.071

Compound: Filterable Particulate

Average

RunNumber 7A-1 7A-2 7A-3

Mass_mg 50.5 41 300.7 130.733

Elb/hr 6.18E+00 4.84E+00 3.56E+01 15.540

gr/dscf 5.35E-03 4.29E-03 3.12E-02 0.014

gr/dscf@7%O2 5.30E-03 4.26E-03 3.10E-02 0.014

lb/mmBtuO2 1.11E-02 8.95E-03 6.50E-02 0.028

mg/dscm 1.23E+01 9.82E+00 7.13E+01 31.140

mg/dscm@7%O2 1.22E+01 9.75E+00 7.08E+01 30.917

ug/dscm 1.23E+04 9.82E+03 7.13E+04 31,140.000

ug/dscm@7%O2 1.22E+04 9.75E+03 7.08E+04 30,916.667

Compound: Lead

Average

RunNumber 7A-1 7A-2 7A-3

Mass_mg 0.00811 0.00916 0.05091 0.023

Elb/hr 9.92E-04 1.08E-03 6.02E-03 0.003

gr/dscf 8.60E-07 9.59E-07 5.27E-06 0.000

gr/dscf@7%O2 8.53E-07 9.52E-07 5.24E-06 0.000

lb/mmBtuO2 1.79E-06 2.00E-06 1.10E-05 0.000

mg/dscm 1.97E-03 2.19E-03 1.21E-02 0.005

mg/dscm@7%O2 1.95E-03 2.17E-03 1.20E-02 0.005

ug/dscm 1.97E+00 2.19E+00 1.21E+01 5.420

ug/dscm@7%O2 1.95E+00 2.17E+00 1.20E+01 5.373

Compound: Manganese

Average

RunNumber 7A-1 7A-2 7A-3

Mass_mg 0.0095 0.013 0.0511 0.025

Elb/hr 1.16E-03 1.54E-03 6.05E-03 0.003

gr/dscf 1.01E-06 1.36E-06 5.29E-06 0.000

gr/dscf@7%O2 1.00E-06 1.35E-06 5.26E-06 0.000

Wednesday, February 02, 2011 Page 13 of 32
lb/mmBtuO2 2.10E-06 2.84E-06 1.11E-05 0.000

mg/dscm 2.30E-03 3.11E-03 1.21E-02 0.006

mg/dscm@7%O2 2.28E-03 3.09E-03 1.20E-02 0.006

ug/dscm 2.30E+00 3.11E+00 1.21E+01 5.837

ug/dscm@7%O2 2.28E+00 3.09E+00 1.20E+01 5.790

Compound: Nickel

Average

RunNumber 7A-1 7A-2 7A-3

Mass_mg 0.0106 0.0086 0.0516 0.024

Elb/hr 1.30E-03 1.02E-03 6.10E-03 0.003

gr/dscf 1.12E-06 9.00E-07 5.35E-06 0.000

gr/dscf@7%O2 1.11E-06 8.94E-07 5.32E-06 0.000

lb/mmBtuO2 2.34E-06 1.88E-06 1.12E-05 0.000

mg/dscm 2.57E-03 2.06E-03 1.22E-02 0.006

mg/dscm@7%O2 2.55E-03 2.05E-03 1.21E-02 0.006

ug/dscm 2.57E+00 2.06E+00 1.22E+01 5.610

ug/dscm@7%O2 2.55E+00 2.05E+00 1.21E+01 5.567

Compound: Selenium

Average

RunNumber 7A-1 7A-2 7A-3

Mass_mg 1.2215 1.2314 1.6514 1.368

Elb/hr 1.49E-01 1.45E-01 1.95E-01 0.163

gr/dscf 1.29E-04 1.29E-04 1.71E-04 0.000

gr/dscf@7%O2 1.28E-04 1.28E-04 1.70E-04 0.000

lb/mmBtuO2 2.70E-04 2.69E-04 3.57E-04 0.000

mg/dscm 2.96E-01 2.95E-01 3.92E-01 0.328

mg/dscm@7%O2 2.93E-01 2.93E-01 3.89E-01 0.325

ug/dscm 2.96E+02 2.95E+02 3.92E+02 327.667

ug/dscm@7%O2 2.93E+02 2.93E+02 3.89E+02 325.000

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Run CTM033-7A-1 CTM033-7A-2 CTM033-7A-3

Elb/hr 7.36E+02 7.42E+02 7.33E+02 737.000

lb/mmBtuO2 1.44E+00 1.45E+00 1.43E+00 1.440

ppm 5.91E+02 5.94E+02 5.89E+02 591.333

ppm@7%O2 5.91E+02 5.91E+02 5.87E+02 589.667

Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run CTM033-7A-1 CTM033-7A-2 CTM033-7A-3

Elb/hr 9.52E+01 1.02E+02 1.02E+02 99.733

lb/mmBtuO2 1.87E-01 1.98E-01 2.00E-01 0.195

ppm 1.06E+02 1.13E+02 1.14E+02 111.000

ppm@7%O2 1.06E+02 1.13E+02 1.14E+02 111.000

Location: Stack Exit - OTM - 27/28

Wednesday, February 02, 2011 Page 14 of 32
Process Run Data

Compound: Filterable PM2.5

Average

RunNumber 7A-1 7A-2 7A-3

Mass_mg 24.7 24.6 110.8 53.367

Elb/hr 3.02E+00 3.50E+00 1.72E+01 7.907

gr/dscf 2.53E-03 2.85E-03 1.43E-02 0.007

gr/dscf@7%O2 2.51E-03 2.83E-03 1.42E-02 0.007

lb/mmBtuO2 5.26E-03 5.95E-03 2.99E-02 0.014

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 7A-1 7A-2 7A-3

Mass_mg 7.5 16.4 29.3 17.733

Elb/hr 9.18E-01 2.33E+00 4.56E+00 2.603

gr/dscf 7.67E-04 1.90E-03 3.79E-03 0.002

gr/dscf@7%O2 7.60E-04 1.89E-03 3.77E-03 0.002

lb/mmBtuO2 1.60E-03 3.97E-03 7.92E-03 0.004

Compound: Organic Condensible Particulate

Average

RunNumber 7A-1 7A-2 7A-3

Mass_mg 71.4 227 126 141.467

Elb/hr 8.74E+00 3.23E+01 1.96E+01 20.213

gr/dscf 7.30E-03 2.63E-02 1.63E-02 0.017

gr/dscf@7%O2 7.24E-03 2.61E-02 1.62E-02 0.017

lb/mmBtuO2 1.52E-02 5.49E-02 3.41E-02 0.035

Compound: Total PM2.5

Average

RunNumber 7A-1 7A-2 7A-3

Mass_mg 103.6 268 266.1 212.567

Elb/hr 1.27E+01 3.81E+01 4.14E+01 30.733

gr/dscf 1.06E-02 3.11E-02 3.45E-02 0.025

gr/dscf@7%O2 1.05E-02 3.09E-02 3.43E-02 0.025

lb/mmBtuO2 2.21E-02 6.48E-02 7.19E-02 0.053

Wednesday, February 02, 2011 Page 15 of 32
Process Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input Million Btus/million BTU using O2 0 0

2 Heat Input Million Btus/million BTU using O2 0 0

3 Heat Input Million Btus/million BTU using O2 0 0

4 Heat Input Million Btus/million BTU using O2 0 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

1 Steam Output 0 1000 lb steam/hr 0

2 Steam Output 0 1000 lb steam/hr 0

3 Steam Output 0 1000 lb steam/hr 0

4 Steam Output 0 1000 lb steam/hr 0

1 Synfuel Firing Rate 0 1000 Tons/hr 0

2 Synfuel Firing Rate 0 1000 Tons/hr 0

3 Synfuel Firing Rate 0 1000 Tons/hr 0

4 Synfuel Firing Rate 0 1000 Tons/hr 0

1 Petroleum Coke Firing Rate 0 1000 Tons/hr 0

2 Petroleum Coke Firing Rate 0 1000 Tons/hr 0

3 Petroleum Coke Firing Rate 0 1000 Tons/hr 0

4 Petroleum Coke Firing Rate 0 1000 Tons/hr 0

1 Coal Gas Firing Rate 0 Ft^3/min 0

2 Coal Gas Firing Rate 0 Ft^3/min 0

3 Coal Gas Firing Rate 0 Ft^3/min 0

4 Coal Gas Firing Rate 0 Ft^3/min 0

1 Fuel Oil Firing Rate 0 gal/hr 0

2 Fuel Oil Firing Rate 0 gal/hr 0

3 Fuel Oil Firing Rate 0 gal/hr 0

4 Fuel Oil Firing Rate 0 gal/hr 0

1 Flue Gas Flow Rate 0 0

4 Flue Gas Flow Rate 0 0

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

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

1 FGD Scrubber Liquor pH 0 pH 0

Wednesday, February 02, 2011 Page 16 of 32
APCD Run Data

Process Lab Run Data

4 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

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

1 Flue Gas Oxygen Content 0 % 0

4 Flue Gas Oxygen Content 0 % 0

1 Flue Gas Carbon Dioxide Content 0 % 0

4 Flue Gas Carbon Dioxide Content 0 % 0

1 Flue Gas Moisture Content 0 % 0

4 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

1 Flue Gas Pressure 0 atm 0

4 Flue Gas Pressure 0 atm 0

1 Standard Pressure 0 atm 0

4 Standard Pressure 0 atm 0

1 Standard Temperature 0 Deg F 0

4 Standard Temperature 0 Deg F 0

1 Unit Gross Electrical Output 0 Mwe 0

4 Unit Gross Electrical Output 0 Mwe 0

1 Unit Net Electric Generation 0 MWh 0

4 Unit Net Electric Generation 0 MWh 0

Run Name Value UOM Comments

Target

Value

1 ELECTROSTATIC PRECIPITATOR 0 0

1 drop down lists. If not on list add description and 

provide detailed

0 0

1 desription in section 5a. 0 0

1 0 0

1 SELECTIVE NONCATALYTIC REDUCTION 

FOR NOX

0 0

Run Name Value UOM Comments

Wednesday, February 02, 2011 Page 17 of 32
Run Name Value UOM Comments

1 Fuel Higher Heating Value 0 Btu/lb

1 Fuel Moisture 0 %

1 Ultimate/Proximate Analysis 0

1 Fuel Chlorine Content 0 mg/kg

1 Fuel Fluorine Content 0 mg/kg

1 Metals Content 0 mg/kg

Wednesday, February 02, 2011 Page 18 of 32
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

Wednesday, February 02, 2011 Page 19 of 32
Location Stack Exit - Method 10 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Wednesday, February 02, 2011 Page 20 of 32
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

Wednesday, February 02, 2011 Page 21 of 32
Location Stack Exit - Method 26A

Average

Run Number CTM033-7A-1 CTM033-

7A-2

CTM033-7A3

Test Date 4/7/2010 4/7/2010 4/7/2010

Run Start Time 9:08:00 AM 10:42:00 AM 12:25:00 PM

Run Finish Time 10:15:00 AM 11:51:00 AM 1:31:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 60 60 60

Nozzle Diameter, inches 0.222 0.222 0.222 0.222

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.016 1.016 1.016 1.016

Barometric Pressure, inches of Mercury 29.28 29.28 29.28 29.280

Average Orifice Meter Differential, inches H2O 1.27 1.31 1.28 1.287

Dry Gas Meter Volume Sampled, cubic feet 37.118 37.785 37.482 37.462

Average Dry Gas Meter Temperature, °F 73.33 80.00 82.92 78.750

Dry Gas Meter Volume Sampled, dscf 36.653 36.854 36.359 36.622

Total Moisture Liquid collected, g 80.5 83.1 77.2 80.267

Volume of Water Vapor, standard cubic feet 3.79 3.91 3.63 3.777

Moisture Content of Stack Gas, % 9.37 9.59 9.08 9.347

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

Dry Mole Fraction 0.9063 0.9041 0.9092 0.907

Carbon Dioxide, % 12.83 12.87 12.82 12.840

Oxygen, % 6.99 6.94 6.95 6.960

Carbon Monoxide & Nitrogen, % 80.18 80.19 80.23 80.200

Fuel Factor 1.08 1.08 1.09

Dry Molecular Weight, lb/lb-Mole 30.33 30.34 30.33 30.333

Wet Molecular weight, lb/lb-Mole 29.17 29.16 29.21 29.180

Flue Gas Static Pressure, inches of H2O -0.92 -0.97 -0.83 -0.907

Absolute Flue Gas Pressure, inches of Mercury 29.21 29.21 29.22 29.213

Average Stack Gas Temperature, °F 320.83 323.42 324.58 322.943

Average Velocity Head, inches of H2O 0.7950321329

54556

0.806009507

672784

0.794240450

629848

0.798

Average Stack Gas Velocity, feet/second 61.30 61.83 61.36 61.497

Stack Cross-Sectional Area, square feet 56.745 56.745 56.745 56.745

Dry Volumetric Flow Rate, dry scfm 124,870.2 125,228.7 124,835.7 124,978.200

Actual Wet Volumetric Flue Gas Flow Rate, acfm 208,708.1 210,512.6 208,912.4 209,377.700

Percent Isokinetic of Sampling Rate, % 103.3 103.5 102.5 103.100

Percent Excess Air, % 49.3 48.8 48.8 48.967

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

Round Duct Diameter, inches 102 102 102

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

Wednesday, February 02, 2011 Page 22 of 32
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

Wednesday, February 02, 2011 Page 23 of 32
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

Wednesday, February 02, 2011 Page 24 of 32
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

Wednesday, February 02, 2011 Page 25 of 32
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

Wednesday, February 02, 2011 Page 26 of 32
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

Wednesday, February 02, 2011 Page 27 of 32
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

Wednesday, February 02, 2011 Page 28 of 32
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

Wednesday, February 02, 2011 Page 29 of 32
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

Wednesday, February 02, 2011 Page 30 of 32
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

Wednesday, February 02, 2011 Page 31 of 32
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

Wednesday, February 02, 2011 Page 32 of 32