Name: Donald Pauken

Title: Manager Environmental Affairs

Company: Muscatine Power and Water

Sign Date: 9/13/2010

Name: Tim Titus

Title: President

Company: Comprehehsive Emission Services, I

Sign Date: 9/13/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Muscatine Power and Water Unit 8 ICR Test

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 23, 2011 Page 1 of 12
Muscatine Power and Water Unit 8 ICR Test

9/13/2010

Facility Information:

Muscatine Power and Water Unit 8

3205 Cedar St.

Muscatine IA 52761

Contact: Donald Pauken

Phone: 563/262-3394

Fax: 563/262-3315

Email: dpauken@mpw.org

Testing Company:

Comprrehensive Emission Services, Inc.

PO Box 910

Waukee IA 50263

Contact:Tim Titus

Phone: 515/987-0200

Fax: 515/987-6604

Email: tim@testces.com

Air Permit Number:

98-TV-021R2

Permitted Source ID/Name:

EP80 Unit 8 Cyclone Boiler

Permitted Maximum Process Rate:

890 million Btu/hr.

Max. Normal Operation Process Rate:

446 million Btu/hr.

Target Process Test Rate

890 million Btu/hr.

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

 process flow diagram:

Unit 8 is a cyclone fired electric generating unit with a nameplate rating of 75 Mwe. The unit burns subbituminous 

coal. Control equipment consists of a cold side electrostaic precipitator (ESP) for particulate control and an overfire 

air system for NOx reduction.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 1913900055 FRS #: 110000415827

SCC / Description 10100223 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Cyclone Furnace (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

Stack exit 114.96 0 0 0 575 230 2 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack exit Total PM2.5 OTM - 27/28 3 240 0

Inorganic (Aqueous) 

Condensible Part.

Stack exit OTM - 27/28 3 240 0

Stack exit Filterable PM2.5 OTM - 27/28 3 240 0

Stack exit Selenium Method 29 3 240 0

Stack exit Nickel Method 29 3 240 0

Stack exit Mercury Method 29 3 240 0

Stack exit Manganese Method 29 3 240 0

Wednesday, February 23, 2011 Page 2 of 12
Muscatine Power and Water Unit 8 ICR Test

9/13/2010

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.

N/A

Stack exit Lead Method 29 3 240 0

Stack exit Cobalt Method 29 3 240 0

Stack exit Chromium Method 29 3 240 0

Stack exit Cadmium Method 29 3 240 0

Stack exit Beryllium Method 29 3 240 0

Stack exit Arsenic Method 29 3 240 0

Stack exit Antimony Method 29 3 240 0

Wednesday, February 23, 2011 Page 3 of 12
Muscatine Power and Water Unit 8 ICR Test

9/13/2010

Sampling / Stack Data Results Summary

Location Stack exit - Method 29

Average

Run Number 1 2 3

Test Date 7/13/2010 7/13/2010 7/14/2010

Run Start Time 8:26:00 AM 1:23:00 PM 8:03:00 AM

Run Finish Time 12:39:00 PM 5:30:00 PM 12:12:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 164.111 164.311 162.784 163.735

Moisture Content of Stack Gas, % 14.16 14.83 15.12 14.703

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

Carbon Dioxide, % 13.93 14 14.45 14.127

Oxygen, % 5.07 4.97 4.93 4.990

Average Stack Gas Temperature, °F 361.88 368.83 365.75 365.487

Dry Volumetric Flow Rate, dry scfm 193,972.1 193,059.3 193,586.1 193,539.167

Actual Wet Volumetric Flue Gas Flow Rate, acfm 353,989.8 358,098.4 358,963.4 357,017.200

Percent Isokinetic of Sampling Rate, % 100.8 101.4 100.2 100.800

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 - 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 23, 2011 Page 4 of 12
Muscatine Power and Water Unit 8 ICR Test

9/13/2010

Wednesday, February 23, 2011 Page 5 of 12
Muscatine Power and Water Unit 8 ICR Test

9/13/2010

Emissions Summary

Location: Stack exit - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.00543 0.00407 0.0046 0.005

Elb/hr 8.49E-04 6.33E-04 7.24E-04 0.001

lb/mmBtuCO2 9.43E-07 7.02E-07 7.76E-07 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.00584 0.00268 0.00579 0.005

Elb/hr 9.13E-04 4.17E-04 9.11E-04 0.001

lb/mmBtuCO2 1.01E-06 4.62E-07 9.77E-07 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.00012 0.00011 0.00012 0.000

Elb/hr 1.88E-05 1.71E-05 1.89E-05 0.000

lb/mmBtuCO2 2.08E-08 1.90E-08 2.02E-08 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.00067 0.00019 0.00072 0.001

Elb/hr 1.05E-04 2.95E-05 1.13E-04 0.000

lb/mmBtuCO2 1.16E-07 3.28E-08 1.21E-07 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.00732 0.00624 0.00435 0.006

Elb/hr 1.14E-03 9.70E-04 6.84E-04 0.001

lb/mmBtuCO2 1.27E-06 1.08E-06 7.34E-07 0.000

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.00437 0.00178 0.00171 0.003

Elb/hr 6.83E-04 2.77E-04 2.69E-04 0.000

lb/mmBtuCO2 7.59E-07 3.07E-07 2.88E-07 0.000

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.00419 0.01017 0.00245 0.006

Elb/hr 6.55E-04 1.58E-03 3.85E-04 0.001

lb/mmBtuCO2 7.27E-07 1.75E-06 4.13E-07 0.000

Wednesday, February 23, 2011 Page 6 of 12
Muscatine Power and Water Unit 8 ICR Test

9/13/2010

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.26693 0.02388 0.05766 0.116

Elb/hr 4.17E-02 3.71E-03 9.07E-03 0.018

lb/mmBtuCO2 4.63E-05 4.12E-06 9.73E-06 0.000

Compound: Mercury

Average

RunNumber 1 2 3

Mass_mg 0.020085 0.0216323 0.020731 0.021

Elb/hr 3.14E-03 3.36E-03 3.26E-03 0.003

lb/mmBtuCO2 3.49E-06 3.73E-06 3.50E-06 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.00874 0.00678 0.00614 0.007

Elb/hr 1.37E-03 1.05E-03 9.66E-04 0.001

lb/mmBtuCO2 1.52E-06 1.17E-06 1.04E-06 0.000

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.03745 0.0188 0.02346 0.027

Elb/hr 5.86E-03 2.92E-03 3.69E-03 0.004

lb/mmBtuCO2 6.50E-06 3.24E-06 3.96E-06 0.000

Location: Stack exit - OTM - 27/28

Compound: Filterable PM2.5

Average

RunNumber 1 2 4

Mass_mg 4.5 9.6 9.3 7.800

Elb/hr 1.54E+00 3.21E+00 3.20E+00 2.650

gr/dscf 8.83E-04 1.87E-03 1.86E-03 0.002

lb/mmBtuCO2 1.63E-03 3.43E-03 3.36E-03 0.003

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 4

Mass_mg 116.7 41.9 46.9 68.500

Elb/hr 3.99E+01 1.40E+01 1.61E+01 23.333

gr/dscf 2.29E-02 8.15E-03 9.40E-03 0.013

lb/mmBtuCO2 4.23E-02 1.50E-02 1.70E-02 0.025

Compound: Total PM2.5

Average

RunNumber 1 2 4

Mass_mg 121.2 51.5 56.3 76.333

Elb/hr 4.14E+01 1.72E+01 1.93E+01 25.967

gr/dscf 2.38E-02 1.00E-02 1.13E-02 0.015

lb/mmBtuCO2 4.39E-02 1.84E-02 2.04E-02 0.028

Wednesday, February 23, 2011 Page 7 of 12
Muscatine Power and Water Unit 8 ICR Test

9/13/2010

Process Run Data

Wednesday, February 23, 2011 Page 8 of 12
Muscatine Power and Water Unit 8 ICR Test

9/13/2010

Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Megawatts (Gross)/Hr. 74 MWG/Hr. 74

2 Megawatts (Gross)/Hr. 74 MWG/Hr. 74

3 Megawatts (Gross)/Hr. 75 MWG/Hr. 74

4 Megawatts (Gross)/Hr. 75 MWG/Hr. 74

1 Heat Input Million Btus/million BTU using CO2 0 0

Run Name Value UOM Comments

Target

Value

1 OVERFIRE AIR 0.836 lb./Mbtu 0.86

2 OVERFIRE AIR 0.83 lb./Mbtu 0.86

3 OVERFIRE AIR 0.791 lb./Mbtu 0.86

4 OVERFIRE AIR 0.756 lb./Mbtu 0.86

1 ELECTROSTATIC PRECIPITATOR 0.0398 lb/MMBtu 0.3

2 ELECTROSTATIC PRECIPITATOR 0.0168 lb/MMBtu 0.3

3 ELECTROSTATIC PRECIPITATOR 0.0185 lb/MMBtu 0.3

4 ELECTROSTATIC PRECIPITATOR 0.0185 lb/MMBtu 0.3

Run Name Value UOM Comments

1 Antimony 9E-07 lb/MMBtu

2 Antimony 7E-07 lb/MMBtu

3 Antimony 7E-07 lb/MMBtu

4 Antimony lb/MMBtu

1 Arsenic 1E-06 lb/MMBtu

2 Arsenic 4E-07 lb/MMBtu

3 Arsenic 9E-07 lb/MMBtu

4 Arsenic lb/MMBtu

1 Beryllium 2E-08 lb/MMBtu

2 Beryllium 2E-08 lb/MMBtu

3 Beryllium 2E-08 lb/MMBtu

4 Beryllium lb/MMBtu

1 Cadmium 1E-07 lb/MMBtu

2 Cadmium 3E-08 lb/MMBtu

3 Cadmium 1E-07 lb/MMBtu

4 Cadmium lb/MMBtu

1 Chromium 1E-06 lb/MMBtu

Wednesday, February 23, 2011 Page 9 of 12
Muscatine Power and Water Unit 8 ICR Test

9/13/2010

2 Chromium 1E-06 lb/MMBtu

3 Chromium 7E-07 lb/MMBtu

4 Chromium lb/MMBtu

1 Cobalt 7E-07 lb/MMBtu

2 Cobalt 3E-07 lb/MMBtu

3 Cobalt 3E-07 lb/MMBtu

4 Cobalt lb/MMBtu

1 Lead 7E-07 lb/MMBtu

2 Lead 2E-06 lb/MMBtu

3 Lead 4E-07 lb/MMBtu

4 Lead lb/MMBtu

1 Manganese 4E-05 lb/MMBtu

2 Manganese 4E-06 lb/MMBtu

3 Manganese 9E-06 lb/MMBtu

4 Manganese lb/MMBtu

1 Mercury 3E-06 lb/MMBtu

2 Mercury 4E-06 lb/MMBtu

3 Mercury 3E-06 lb/MMBtu

4 Mercury lb/MMBtu

1 Nickel 1E-06 lb/MMBtu

2 Nickel 1E-06 lb/MMBtu

3 Nickel 1E-06 lb/MMBtu

4 Nickel lb/MMBtu

1 Selenium 6E-06 lb/MMBtu

2 Selenium 3E-06 lb/MMBtu

3 Selenium 4E-06 lb/MMBtu

4 Selenium lb/MMBtu

1 PM2.5 0.04 lb/MMBtu

2 PM2.5 0.017 lb/MMBtu

3 PM2.5 0.019 lb/MMBtu

4 PM2.5 0.019 lb/MMBtu

Wednesday, February 23, 2011 Page 10 of 12
Muscatine Power and Water Unit 8 ICR Test

9/13/2010

Sampling / Stack Data Results Detail

Location Stack exit - Method 29

Average

Run Number 1 2 3

Test Date 7/13/2010 7/13/2010 7/14/2010

Run Start Time 8:26:00 AM 1:23:00 PM 8:03:00 AM

Run Finish Time 12:39:00 PM 5:30:00 PM 12:12:00 PM

Net Traversing Points 24 24 24

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 0.991 0.991 0.991 0.991

Barometric Pressure, inches of Mercury 29.69 29.69 29.69 29.690

Average Orifice Meter Differential, inches H2O 1.83 1.85 1.87 1.850

Dry Gas Meter Volume Sampled, cubic feet 174.410 175.042 172.598 174.017

Average Dry Gas Meter Temperature, °F 94.31 95.67 93.08 94.353

Dry Gas Meter Volume Sampled, dscf 164.111 164.311 162.784 163.735

Total Moisture Liquid collected, g 575 608 616 599.667

Volume of Water Vapor, standard cubic feet 27.07 28.62 29.00 28.230

Moisture Content of Stack Gas, % 14.16 14.83 15.12 14.703

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

Dry Mole Fraction 0.8584 0.8517 0.8488 0.853

Carbon Dioxide, % 13.93 14 14.45 14.127

Oxygen, % 5.07 4.97 4.93 4.990

Carbon Monoxide & Nitrogen, % 81 81.03 80.62 80.883

Fuel Factor 1.14 1.14 1.11

Dry Molecular Weight, lb/lb-Mole 30.43 30.44 30.51 30.460

Wet Molecular weight, lb/lb-Mole 28.67 28.60 28.62 28.630

Flue Gas Static Pressure, inches of H2O 0.51 0.51 0.51 0.510

Absolute Flue Gas Pressure, inches of Mercury 29.73 29.73 29.73 29.730

Average Stack Gas Temperature, °F 361.88 368.83 365.75 365.487

Average Velocity Head, inches of H2O 1.3472573549

3078

1.363699007

65272

1.376449923

30445

1.362

Average Stack Gas Velocity, feet/second 81.85 82.80 83.00 82.550

Stack Cross-Sectional Area, square feet 72.081 72.081 72.081 72.081

Dry Volumetric Flow Rate, dry scfm 193,972.1 193,059.3 193,586.1 193,539.167

Actual Wet Volumetric Flue Gas Flow Rate, acfm 353,989.8 358,098.4 358,963.4 357,017.200

Percent Isokinetic of Sampling Rate, % 100.8 101.4 100.2 100.800

Percent Excess Air, % 31.1 30.3 30.1 30.500

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

Round Duct Diameter, inches 114.96 114.96 114.96

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 23, 2011 Page 11 of 12
Muscatine Power and Water Unit 8 ICR Test

9/13/2010

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 23, 2011 Page 12 of 12