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: 9/30/2010

Permitted Facility Representative / Date Testing Company Representative / Date

MO2161 James River 4

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 14
MO2161 James River 4

9/30/2010

Facility Information:

MO2161 James River 4

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:

4 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 JR4 144 0 0 0 0 0 4 16

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

MO2161 JR4 Carbon Monoxide Method 10 3 120 0

Total organic compounds 

(TOC) as Propane

MO2161 JR4 Method 25A 3 120 0

MO2161 JR4 Total PM2.5 OTM - 27/28 3 330 0

Organic Condensible 

Particulate

MO2161 JR4 OTM - 27/28 3 330 0

Inorganic (Aqueous) 

Condensible Part.

MO2161 JR4 OTM - 27/28 3 330 0

Saturday, January 29, 2011 Page 2 of 14
MO2161 James River 4

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 JR4 Filterable PM2.5 OTM - 27/28 3 330 0

MO2161 JR4 Filterable Particulate Method 29 3 240 0

MO2161 JR4 Selenium Method 29 3 240 0

MO2161 JR4 Nickel Method 29 3 240 0

MO2161 JR4 Manganese Method 29 3 240 0

MO2161 JR4 Antimony Method 29 3 240 0

MO2161 JR4 Arsenic Method 29 3 240 0

MO2161 JR4 Cobalt Method 29 3 240 0

MO2161 JR4 Chromium Method 29 3 240 0

MO2161 JR4 Beryllium Method 29 3 240 0

MO2161 JR4 Cadmium Method 29 3 240 0

MO2161 JR4 Mercury Method 29 3 240 0

MO2161 JR4 Lead Method 29 3 240 0

Saturday, January 29, 2011 Page 3 of 14
MO2161 James River 4

9/30/2010

Sampling / Stack Data Results Summary

Location MO2161 JR4 - 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 MO2161 JR4 - 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

Saturday, January 29, 2011 Page 4 of 14
MO2161 James River 4

9/30/2010

Location MO2161 JR4 - Method 29

Average

Run Number M29-1 M29-2 M29-4

Test Date 6/22/2010 6/23/2010 6/24/2010

Run Start Time 11:15:00 AM 6:00:00 

AM

11:43:00 AM

Run Finish Time 3:07:30 PM 9:52:30 

AM

3:35:30 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 129.545 128.815 129.206 129.189

Moisture Content of Stack Gas, % 13.62 15.16 13.68 14.153

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

Carbon Dioxide, % 12.1 12.3 12.7 12.367

Oxygen, % 7.4 7.2 7 7.200

Average Stack Gas Temperature, °F 329.78 313.44 313.06 318.760

Dry Volumetric Flow Rate, dry scfm 146,751.7 144,006.3 148,982.6 146,580.200

Actual Wet Volumetric Flue Gas Flow Rate, acfm 265,664.9 260,846.9 263,900.5 263,470.767

Percent Isokinetic of Sampling Rate, % 100.9 102.2 99.1 100.733

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 MO2161 JR4 - 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

Saturday, January 29, 2011 Page 5 of 14
MO2161 James River 4

9/30/2010

Saturday, January 29, 2011 Page 6 of 14
MO2161 James River 4

9/30/2010

Emissions Summary

Location: MO2161 JR4 - Method 10

Compound: Carbon Monoxide

Average

Run M10-1 M10-2 M10-3

lb/mmBtuO2 1.16E-01 1.79E-01 1.50E-01 0.148

ppm 1.07E+02 1.66E+02 1.41E+02 138.000

ppm@7%O2 1.08E+02 1.67E+02 1.40E+02 138.333

Location: MO2161 JR4 - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run M25A-1 M25A-2 M25A-3

lb/mmBtuO2 5.85E-05 1.76E-04 1.45E-04 0.000

ppm 3.45E-02 1.04E-01 8.69E-02 0.075

ppm@7%O2 3.48E-02 1.05E-01 8.63E-02 0.075

Location: MO2161 JR4 - Method 29

Compound: Antimony

Average

RunNumber M29-1 M29-2 M29-4

Mass_mg 0.0048 0.0028 0.0028 0.003

lb/mmBtuO2 1.24E-06 7.15E-07 7.03E-07 0.000

Compound: Arsenic

Average

RunNumber M29-1 M29-2 M29-4

Mass_mg 0.01115 0.00688 0.00631 0.008

lb/mmBtuO2 2.87E-06 1.76E-06 1.58E-06 0.000

Compound: Beryllium

Average

RunNumber M29-1 M29-2 M29-4

Mass_mg 0.00146 0.00087 0.00078 0.001

lb/mmBtuO2 3.76E-07 2.22E-07 1.96E-07 0.000

Compound: Cadmium

Average

RunNumber M29-1 M29-2 M29-4

Mass_mg 0.00506 0.00101 0.00095 0.002

lb/mmBtuO2 1.30E-06 2.58E-07 2.38E-07 0.000

Compound: Chromium

Average

RunNumber M29-1 M29-2 M29-4

Mass_mg 0.20539 1.4984 0.12474 0.610

lb/mmBtuO2 5.29E-05 3.83E-04 3.13E-05 0.000

Compound: Cobalt

Average

RunNumber M29-1 M29-2 M29-4

Saturday, January 29, 2011 Page 7 of 14
MO2161 James River 4

9/30/2010

Mass_mg 0.01355 0.03877 0.0059 0.019

lb/mmBtuO2 3.49E-06 9.90E-06 1.48E-06 0.000

Compound: Filterable Particulate

Average

RunNumber M29-1 M29-2 M29-4

Mass_mg 62.4 83.4 83.4 76.400

lb/mmBtuO2 1.61E-02 2.13E-02 2.09E-02 0.019

Compound: Lead

Average

RunNumber M29-1 M29-2 M29-4

Mass_mg 32.51279 0.02139 0.19259 10.909

lb/mmBtuO2 8.38E-03 5.46E-06 4.83E-05 0.003

Compound: Manganese

Average

RunNumber M29-1 M29-2 M29-4

Mass_mg 0.10225 0.30655 0.04035 0.150

lb/mmBtuO2 2.63E-05 7.83E-05 1.01E-05 0.000

Compound: Mercury

Average

RunNumber M29-1 M29-2 M29-4

Mass_mg 0.01074 0.01091 0.01044 0.011

lb/mmBtuO2 2.77E-06 2.79E-06 2.62E-06 0.000

Compound: Nickel

Average

RunNumber M29-1 M29-2 M29-4

Mass_mg 0.42278 1.79288 0.18198 0.799

lb/mmBtuO2 1.09E-04 4.58E-04 4.57E-05 0.000

Compound: Selenium

Average

RunNumber M29-1 M29-2 M29-4

Mass_mg 0.0222 0.0385 0.0171 0.026

lb/mmBtuO2 5.72E-06 9.83E-06 4.29E-06 0.000

Location: MO2161 JR4 - OTM - 27/28

Compound: Filterable PM2.5

Average

RunNumber OTM27-1 OTM27-2 OTM27-3

Mass_mg 46.8 64.3 45.6 52.233

lb/mmBtuO2 1.33E-02 1.76E-02 1.25E-02 0.014

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber OTM27-1 OTM27-2 OTM27-3

Mass_mg 94 97 78 89.667

lb/mmBtuO2 2.66E-02 2.66E-02 2.14E-02 0.025

Saturday, January 29, 2011 Page 8 of 14
MO2161 James River 4

9/30/2010

Process Run Data

Compound: Organic Condensible Particulate

Average

RunNumber OTM27-1 OTM27-2 OTM27-3

Mass_mg 4.9 3.5 4.7 4.367

lb/mmBtuO2 1.39E-03 9.59E-04 1.29E-03 0.001

Compound: Total PM2.5

Average

RunNumber OTM27-1 OTM27-2 OTM27-3

Mass_mg 145.7 164.8 128.3 146.267

lb/mmBtuO2 4.13E-02 4.52E-02 3.53E-02 0.041

Saturday, January 29, 2011 Page 9 of 14
MO2161 James River 4

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 536.5 Daily Average (6-

22-10)

0

2 Heat Input Million Btus/million BTU using O2 541.6 Daily Average (6-

23-10)

0

3 Heat Input Million Btus/million BTU using O2 540 Daily Average (6-

24-10)

0

1 Unit Load 55.5 MW Daily Average (6-

22-10)

0

2 Unit Load 56.6 MW Daily Average (6-

23-10)

0

3 Unit Load 56.6 MW Daily Average (6-

24-10)

0

1 Steam Rate 415.1 1000 lbs/hr Daily Average (6-

22-10)

0

2 Steam Rate 429.9 1000 lbs/hr Daily Average (6-

23-10)

0

3 Steam Rate 428.3 1000 lbs/hr Daily Average (6-

24-10)

0

1 Fuel Rate 31.7 tons/hr Daily Average (6-

22-10)

0

2 Fuel Rate 32 tons/hr Daily Average (6-

23-10)

0

3 Fuel Rate 32 tons/hr Daily Average (6-

24-10)

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 10 of 14
MO2161 James River 4

9/30/2010

Sampling / Stack Data Results Detail

Location MO2161 JR4 - 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 29, 2011 Page 11 of 14
MO2161 James River 4

9/30/2010

Location MO2161 JR4 - 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 29, 2011 Page 12 of 14
MO2161 James River 4

9/30/2010

Location MO2161 JR4 - Method 29

Average

Run Number M29-1 M29-2 M29-4

Test Date 6/22/2010 6/23/2010 6/24/2010

Run Start Time 11:15:00 AM 6:00:00 AM 11:43:00 AM

Run Finish Time 3:07:30 PM 9:52:30 AM 3:35:30 PM

Net Traversing Points 32 32 32

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.275 0.275 0.275 0.275

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.99 0.99 1.01 0.997

Barometric Pressure, inches of Mercury 28.65 28.55 28.68 28.627

Average Orifice Meter Differential, inches H2O 0.93 0.91 0.95 0.930

Dry Gas Meter Volume Sampled, cubic feet 144.780 141.944 139.856 142.193

Average Dry Gas Meter Temperature, °F 100.73 90.91 94.66 95.433

Dry Gas Meter Volume Sampled, dscf 129.545 128.815 129.206 129.189

Total Moisture Liquid collected, g 434 489 435 452.667

Volume of Water Vapor, standard cubic feet 20.43 23.02 20.48 21.310

Moisture Content of Stack Gas, % 13.62 15.16 13.68 14.153

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

Dry Mole Fraction 0.8638 0.8484 0.8632 0.858

Carbon Dioxide, % 12.1 12.3 12.7 12.367

Oxygen, % 7.4 7.2 7 7.200

Carbon Monoxide & Nitrogen, % 80.5 80.5 80.3 80.433

Fuel Factor 1.12 1.11 1.09

Dry Molecular Weight, lb/lb-Mole 30.23 30.26 30.31 30.267

Wet Molecular weight, lb/lb-Mole 28.56 28.40 28.63 28.530

Flue Gas Static Pressure, inches of H2O -0.35 -0.35 -0.35 -0.350

Absolute Flue Gas Pressure, inches of Mercury 28.62 28.52 28.65 28.597

Average Stack Gas Temperature, °F 329.78 313.44 313.06 318.760

Average Velocity Head, inches of H2O 0.3075404436

33086

0.299997101

221617

0.311239203

777391

0.306

Average Stack Gas Velocity, feet/second 39.15 38.44 38.89 38.827

Stack Cross-Sectional Area, square feet 113.097 113.097 113.097 113.097

Dry Volumetric Flow Rate, dry scfm 146,751.7 144,006.3 148,982.6 146,580.200

Actual Wet Volumetric Flue Gas Flow Rate, acfm 265,664.9 260,846.9 263,900.5 263,470.767

Percent Isokinetic of Sampling Rate, % 100.9 102.2 99.1 100.733

Percent Excess Air, % 53.4 51.2 49.3 51.300

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

Round Duct Diameter, inches 144 144 144

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 13 of 14
MO2161 James River 4

9/30/2010

Location MO2161 JR4 - 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

Saturday, January 29, 2011 Page 14 of 14