Name: David M. Fraley, Ph.D.

Title: Director - Environmental Affairs

Company: City Utilities of Springfield

Sign Date: 9/30/2010

Name: Mike Taylor

Title: President

Company: Catalyst Air Management

Sign Date: 9/29/2010

Permitted Facility Representative / Date Testing Company Representative / Date

MO2161 James River 5

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 29, 2011 Page 1 of 10
MO2161 James River 5

9/30/2010

Facility Information:

MO2161 James River 5

5701 South Kissick Rd

Springfield MO 65804

Contact: Daniel Hedrick

Phone: 417-831-8916

Fax:

Email: daniel.hedrick@cityutilities.net

Testing Company:

Catalyst Air Management

2505 ByingRdton-Solway

Knoxville TN 37931

Contact:Mike Taylor

Phone: 865-531-0075

Fax: 865-531-0750

Email: mike.taylor@catalystair.com

Air Permit Number:

2161

Permitted Source ID/Name:

5 City Utilities of Springfield James River Station

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

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

 process flow diagram:

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: FRS #:

SCC / Description 10100222 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Pulverized Coal: Dry Bottom (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

MO2161 JR5 123 0 0 0 0 0 4 16

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

MO2161 JR5 Total PM2.5 OTM - 27/28 3 362 0

Organic Condensible 

Particulate

MO2161 JR5 OTM - 27/28 3 362 0

Inorganic (Aqueous) 

Condensible Part.

MO2161 JR5 OTM - 27/28 3 362 0

MO2161 JR5 Filterable PM2.5 OTM - 27/28 3 362 0

MO2161 JR5 Lead Method 29 3 240 0

MO2161 JR5 Selenium Method 29 3 240 0

Saturday, January 29, 2011 Page 2 of 10
MO2161 James River 5

9/30/2010

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.

MO2161 JR5 Nickel Method 29 3 240 0

MO2161 JR5 Manganese Method 29 3 240 0

MO2161 JR5 Cadmium Method 29 3 240 0

MO2161 JR5 Antimony Method 29 3 240 0

MO2161 JR5 Filterable Particulate Method 29 3 240 0

MO2161 JR5 Arsenic Method 29 3 240 0

MO2161 JR5 Cobalt Method 29 3 240 0

MO2161 JR5 Chromium Method 29 3 240 0

MO2161 JR5 Beryllium Method 29 3 240 0

MO2161 JR5 Mercury Method 29 3 240 0

Saturday, January 29, 2011 Page 3 of 10
MO2161 James River 5

9/30/2010

Sampling / Stack Data Results Summary

Location MO2161 JR5 - Method 29

Average

Run Number M29-1 M29-2 M29-3

Test Date 4/26/2010 4/27/2010 4/27/2010

Run Start Time 10:00:00 AM 6:06:00 

AM

10:30:00 AM

Run Finish Time 2:15:00 PM 10:17:00 

AM

2:45:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 179.572 180.325 179.605 179.834

Moisture Content of Stack Gas, % 9.62 10.61 10.47 10.233

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

Carbon Dioxide, % 11.6 11.7 11.5 11.600

Oxygen, % 7.3 7.8 7.7 7.600

Average Stack Gas Temperature, °F 339.06 336.13 343.06 339.417

Dry Volumetric Flow Rate, dry scfm 261,438.1 260,142.9 258,965.3 260,182.100

Actual Wet Volumetric Flue Gas Flow Rate, acfm 462,172.1 462,617.7 463,805.9 462,865.233

Percent Isokinetic of Sampling Rate, % 93.7 94.5 94.6 94.267

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

Saturday, January 29, 2011 Page 4 of 10
MO2161 James River 5

9/30/2010

Location MO2161 JR5 - OTM - 27/28

Average

Run Number OTM27-1 OTM27-2 OTM27-3

Test Date 4/26/2010 4/27/2010 4/27/2010

Run Start Time 10:00:00 AM 6:06:00 

AM

1:07:00 PM

Run Finish Time 4:12:00 PM 12:19:00 

PM

7:16:00 PM

Net Run Time, minutes 360.75 360.75 360.75

Dry Gas Meter Volume Sampled, dscf 118.329 123.955 127.549 123.278

Moisture Content of Stack Gas, % 9.10 10.18 10.26 9.847

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

Carbon Dioxide, % 11.8 11.6 12.9 12.100

Oxygen, % 7.3 8 6.3 7.200

Average Stack Gas Temperature, °F 338.58 334.67 338.17 337.140

Dry Volumetric Flow Rate, dry scfm 262,339.3 260,613.3 259,267.3 260,739.967

Actual Wet Volumetric Flue Gas Flow Rate, acfm 460,835.4 460,389.8 460,439.3 460,554.833

Percent Isokinetic of Sampling Rate, % 84.1 88.7 91.7 88.167

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

Saturday, January 29, 2011 Page 5 of 10
MO2161 James River 5

9/30/2010

Emissions Summary

Location: MO2161 JR5 - Method 29

Compound: Antimony

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.006 0.006 0.006 0.006

lb/mmBtuO2 1.11E-06 1.14E-06 1.14E-06 0.000

Compound: Arsenic

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.0181 0.0145 0.0088 0.014

lb/mmBtuO2 3.34E-06 2.77E-06 1.67E-06 0.000

Compound: Beryllium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.0015 0.00166 0.00151 0.002

lb/mmBtuO2 2.77E-07 3.17E-07 2.87E-07 0.000

Compound: Cadmium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.01024 0.0049 0.00354 0.006

lb/mmBtuO2 1.89E-06 9.35E-07 6.73E-07 0.000

Compound: Chromium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 7.74255 4.59685 1.04465 4.461

lb/mmBtuO2 1.43E-03 8.77E-04 1.99E-04 0.001

Compound: Cobalt

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.09883 0.05594 0.01629 0.057

lb/mmBtuO2 1.82E-05 1.07E-05 3.10E-06 0.000

Compound: Filterable Particulate

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 96.4 80.6 103.9 93.633

lb/mmBtuO2 1.78E-02 1.54E-02 1.97E-02 0.018

Compound: Lead

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.083 0.0462 0.1705 0.100

lb/mmBtuO2 1.53E-05 8.81E-06 3.24E-05 0.000

Compound: Manganese

Average

Saturday, January 29, 2011 Page 6 of 10
MO2161 James River 5

9/30/2010

Process Run Data

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.70826 0.44316 0.11926 0.424

lb/mmBtuO2 1.31E-04 8.45E-05 2.27E-05 0.000

Compound: Mercury

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.01148 0.01398 0.00944 0.012

lb/mmBtuO2 2.12E-06 2.67E-06 1.79E-06 0.000

Compound: Nickel

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 4.85212 3.17692 0.70162 2.910

lb/mmBtuO2 8.95E-04 6.06E-04 1.33E-04 0.001

Compound: Selenium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.1955 0.1422 0.034 0.124

lb/mmBtuO2 3.61E-05 2.71E-05 6.46E-06 0.000

Location: MO2161 JR5 - OTM - 27/28

Compound: Filterable PM2.5

Average

RunNumber OTM27-1 OTM27-2 OTM27-3

Mass_mg 80.36 75.06 94.66 83.360

lb/mmBtuO2 2.25E-02 2.12E-02 2.29E-02 0.022

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber OTM27-1 OTM27-2 OTM27-3

Mass_mg 330 53 36 139.667

lb/mmBtuO2 9.24E-02 1.49E-02 8.71E-03 0.039

Compound: Organic Condensible Particulate

Average

RunNumber OTM27-1 OTM27-2 OTM27-3

Mass_mg 2.7 2.1 2.2 2.333

lb/mmBtuO2 7.56E-04 5.92E-04 5.32E-04 0.001

Compound: Total PM2.5

Average

RunNumber OTM27-1 OTM27-2 OTM27-3

Mass_mg 413.06 130.16 132.86 225.360

lb/mmBtuO2 1.16E-01 3.67E-02 3.22E-02 0.062

Saturday, January 29, 2011 Page 7 of 10
MO2161 James River 5

9/30/2010

Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input Million Btus/million BTU using O2 944.1 Daily Average (4-

26-10)

0

1 Unit Load 91.6 MW Daily Average (4-

26-10)

0

1 Steam Rate 604.6 1000 lbs/hr Daily Average (4-

26-10)

0

1 Fuel Rate 53.6 tons/hr Daily Average (4-

26-10)

0

2 Heat Input Million Btus/million BTU using O2 1012 Daily Average (4-

27-10)

0

2 Unit Load 97.7 MW Daily Average (4-

27-10)

0

2 Steam Rate 646.8 1000 lbs/hr Daily Average (4-

27-10)

0

2 Fuel Rate 57.5 tons/hr Daily Average (4-

27-10)

0

3 Heat Input Million Btus/million BTU using O2 1036.3 Daily Average (4-

28-10)

0

3 Unit Load 99.5 MW Daily Average (4-

28-10)

0

3 Steam Rate 662.7 1000 lbs/hr Daily Average (4-

28-10)

0

3 Fuel Rate 59.2 tons/hr Daily Average (4-

28-10)

0

Run Name Value UOM Comments

Target

Value

1 OVERFIRE AIR 0 0

1 NSCR (NON-SELECTIVE CATALYTIC 

REDUCTION)

0 0

1 ELECTROSTATIC PRECIPITATOR 0 0

Saturday, January 29, 2011 Page 8 of 10
MO2161 James River 5

9/30/2010

Sampling / Stack Data Results Detail

Location MO2161 JR5 - Method 29

Average

Run Number M29-1 M29-2 M29-3

Test Date 4/26/2010 4/27/2010 4/27/2010

Run Start Time 10:00:00 AM 6:06:00 AM 10:30:00 AM

Run Finish Time 2:15:00 PM 10:17:00 AM 2:45:00 PM

Net Traversing Points 16 16 16

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.215 0.215 0.215 0.215

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.01 1.01 1.01 1.010

Barometric Pressure, inches of Mercury 28.15 28.2 28.2 28.183

Average Orifice Meter Differential, inches H2O 1.93 1.94 1.91 1.927

Dry Gas Meter Volume Sampled, cubic feet 190.119 187.751 190.394 189.421

Average Dry Gas Meter Temperature, °F 73.88 65.97 75.47 71.773

Dry Gas Meter Volume Sampled, dscf 179.572 180.325 179.605 179.834

Total Moisture Liquid collected, g 406.3 454.6 446.3 435.733

Volume of Water Vapor, standard cubic feet 19.12 21.40 21.01 20.510

Moisture Content of Stack Gas, % 9.62 10.61 10.47 10.233

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

Dry Mole Fraction 0.9038 0.8939 0.8953 0.898

Carbon Dioxide, % 11.6 11.7 11.5 11.600

Oxygen, % 7.3 7.8 7.7 7.600

Carbon Monoxide & Nitrogen, % 81.1 80.5 80.8 80.800

Fuel Factor 1.17 1.12 1.15

Dry Molecular Weight, lb/lb-Mole 30.15 30.18 30.15 30.160

Wet Molecular weight, lb/lb-Mole 28.98 28.89 28.88 28.917

Flue Gas Static Pressure, inches of H2O 2.6 2.5 2.5 2.533

Absolute Flue Gas Pressure, inches of Mercury 28.34 28.38 28.38 28.367

Average Stack Gas Temperature, °F 339.06 336.13 343.06 339.417

Average Velocity Head, inches of H2O 1.7368812540

274

1.743729401

59308

1.736881254

0274

1.739

Average Stack Gas Velocity, feet/second 93.35 93.44 93.68 93.490

Stack Cross-Sectional Area, square feet 82.516 82.516 82.516 82.516

Dry Volumetric Flow Rate, dry scfm 261,438.1 260,142.9 258,965.3 260,182.100

Actual Wet Volumetric Flue Gas Flow Rate, acfm 462,172.1 462,617.7 463,805.9 462,865.233

Percent Isokinetic of Sampling Rate, % 93.7 94.5 94.6 94.267

Percent Excess Air, % 51.7 58.0 56.5 55.400

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

Round Duct Diameter, inches 123 123 123

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

Saturday, January 29, 2011 Page 9 of 10
MO2161 James River 5

9/30/2010

Location MO2161 JR5 - OTM - 27/28

Average

Run Number OTM27-1 OTM27-2 OTM27-3

Test Date 4/26/2010 4/27/2010 4/27/2010

Run Start Time 10:00:00 AM 6:06:00 AM 1:07:00 PM

Run Finish Time 4:12:00 PM 12:19:00 PM 7:16:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 360.75 360.75 360.75

Nozzle Diameter, inches 0.15 0.15 0.15 0.150

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.02 1.02 1.02 1.020

Barometric Pressure, inches of Mercury 28.15 28.2 28.2 28.183

Average Orifice Meter Differential, inches H2O 0.38 0.38 0.40 0.387

Dry Gas Meter Volume Sampled, cubic feet 123.074 125.840 132.306 127.073

Average Dry Gas Meter Temperature, °F 67.54 55.83 67.08 63.483

Dry Gas Meter Volume Sampled, dscf 118.329 123.955 127.549 123.278

Total Moisture Liquid collected, g 251.7 298.4 309.8 286.633

Volume of Water Vapor, standard cubic feet 11.85 14.05 14.58 13.493

Moisture Content of Stack Gas, % 9.10 10.18 10.26 9.847

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

Dry Mole Fraction 0.909 0.8982 0.8974 0.902

Carbon Dioxide, % 11.8 11.6 12.9 12.100

Oxygen, % 7.3 8 6.3 7.200

Carbon Monoxide & Nitrogen, % 80.9 80.4 80.8 80.700

Fuel Factor 1.15 1.11 1.13

Dry Molecular Weight, lb/lb-Mole 30.18 30.18 30.32 30.227

Wet Molecular weight, lb/lb-Mole 29.07 28.94 29.06 29.023

Flue Gas Static Pressure, inches of H2O 2.6 2.5 2.5 2.533

Absolute Flue Gas Pressure, inches of Mercury 28.34 28.38 28.38 28.367

Average Stack Gas Temperature, °F 338.58 334.67 338.17 337.140

Average Velocity Head, inches of H2O 1.7331128591

4295

1.733112859

14295

1.733112859

14295

1.733

Average Stack Gas Velocity, feet/second 93.08 92.99 93.00 93.023

Stack Cross-Sectional Area, square feet 82.516 82.516 82.516 82.516

Dry Volumetric Flow Rate, dry scfm 262,339.3 260,613.3 259,267.3 260,739.967

Actual Wet Volumetric Flue Gas Flow Rate, acfm 460,835.4 460,389.8 460,439.3 460,554.833

Percent Isokinetic of Sampling Rate, % 84.1 88.7 91.7 88.167

Percent Excess Air, % 51.9 60.5 41.9 51.433

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

Round Duct Diameter, inches 123 123 123

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

Saturday, January 29, 2011 Page 10 of 10