Name: Jim Ward

Title: EHS Manager

Company: Red Hills Power Plant

Sign Date: 8/2/2010

Name: Jeremy Hutchens

Title: Senior Project Manager

Company: Alliance Source Testing, LLC

Sign Date: 8/2/2010

Permitted Facility Representative / Date Testing Company Representative / Date

GDF Suez/RHPP - Ackerman, MS - 2010 Power MACT ICR

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.

Thursday, February 10, 2011 Page 1 of 25
GDF Suez/RHPP - Ackerman, MS - 2010 Power MACT ICR

8/2/2010

Facility Information:

Red Hills Generating Facility

2391 Pensacola Road

PO Box 358

Ackerman MS 39735

Contact: Jim Ward

Phone: (662) 387-4175, ext. 234

Fax:

Email: jim.ward@gdfsuezna.com

Testing Company:

Alliance Source Testing, LLC

214 Central Circle SW

Decatur AL 35603

Contact:Jeremy Hutchens

Phone: (256) 260-3974

Fax: (256) 351-0151

Email: jeremy.hutchens@stacktest.com

Air Permit Number:

55076

Permitted Source ID/Name:

AA002 Boiler No. 2

Permitted Maximum Process Rate:

1,600-1,800 KPPH

Max. Normal Operation Process Rate:

1,600-1,800 KPPH

Target Process Test Rate

1,600-1,800 KPPH

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

 process flow diagram:

RHPP is a single unit lignite-fueled electrical generation facility that supplies electricity to the Tennessee Valley 

Authority (TVA) electrical system. Operations at the facility include lignite processing (e.g., conveying, crushing, 

sizing, and temporary storage of lignite), steam production (e.g., two (2) 250 MW (lignite fueled) Circulating 

Fluidized Bed (CFB) Boilers), electrical power generation (e.g., 440 MW steam turbine generator), limestone 

handling and drying, water treatment (e.g., chemical treatment and cooling towers) for process makeup water, 

handling and onsite disposal of ash. Emissions from each boiler are exhaust from a single common stack.

Industry/SCC/NAIS

Sampling Location Information:

Test Parameter Information:

AFS #: FRS #:

SCC / Description 10100318 External Combustion Boilers - Electric Generation - Lignite - Atmospheric 

Fluidized Bed Combustion - Circulating Bed 

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

Common Stack 216 0 0 0 2160 480 4 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Common StackCarbon Monoxide Method 10 3 180 0

Total organic compounds 

(TOC) as Propane

Common Stack Method 25A 3 180 0

Common Stack Filterable PM2.5 OTM - 27/28 3 420 0

Thursday, February 10, 2011 Page 2 of 25
GDF Suez/RHPP - Ackerman, MS - 2010 Power MACT ICR

8/2/2010

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.

The attached test report provides full methodology descriptions.

Organic Condensible 

Particulate

Common Stack OTM - 27/28 3 420 0

Common Stack Arsenic Method 29 3 420 0

Common Stack Antimony Method 29 3 420 0

Common Stack Mercury Method 29 3 420 0

Common StackBeryllium Method 29 3 420 0

Common StackCadmium Method 29 3 420 0

Common StackChromium Method 29 3 420 0

Common StackCobalt Method 29 3 420 0

Common Stack Lead Method 29 3 420 0

Common Stack Manganese Method 29 3 420 0

Common Stack Nickel Method 29 3 420 0

Common Stack Selenium Method 29 3 420 0

Common Stack Filterable Particulate Method 29 3 420 0

Common Stack O2 Method 3A O2 3 180 0

Common StackCo2 Method 3A CO2 3 180 0

Common Stack Sulfur Dioxide Method 6C 3 180 0

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

Thursday, February 10, 2011 Page 3 of 25
GDF Suez/RHPP - Ackerman, MS - 2010 Power MACT ICR

8/2/2010

Sampling / Stack Data Results Summary

Location Common Stack - 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 Common Stack - 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

Thursday, February 10, 2011 Page 4 of 25
GDF Suez/RHPP - Ackerman, MS - 2010 Power MACT ICR

8/2/2010

Location Common Stack - Method 29

Average

Run Number 3 1 2

Test Date 5/21/2010 5/19/2010 5/20/2010

Run Start Time 7:30:00 AM 9:11:00 

AM

7:14:00 AM

Run Finish Time 5:22:00 PM 6:09:00 PM 4:34:00 PM

Net Run Time, minutes 420 420 420

Dry Gas Meter Volume Sampled, dscf 251.456 248.307 248.090 249.284

Moisture Content of Stack Gas, % 19.25 18.73 19.34 19.107

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

Carbon Dioxide, % 13.8 13.8 13.7 13.767

Oxygen, % 5.3 5.3 5.1 5.233

Average Stack Gas Temperature, °F 304.00 312.08 305.42 307.167

Dry Volumetric Flow Rate, dry scfm 603,310.4 604,095.8 599,460.8 602,289.000

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,096,099.8 1,101,290.9 1,094,573.0 1,097,321.23

3

Percent Isokinetic of Sampling Rate, % 101.1 99.7 100.4 100.400

F-Factor, dscfm/MMBtu @ %O2 9860 9860 9860 9,860.000

Fw 11950 11950 11950 11,950.000

Fc 1910 1910 1910 1,910.000

Location Common Stack - 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

Thursday, February 10, 2011 Page 5 of 25
GDF Suez/RHPP - Ackerman, MS - 2010 Power MACT ICR

8/2/2010

Location Common Stack - 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 Common Stack - 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

Thursday, February 10, 2011 Page 6 of 25
GDF Suez/RHPP - Ackerman, MS - 2010 Power MACT ICR

8/2/2010

Location Common Stack - 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 Common Stack - 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

Thursday, February 10, 2011 Page 7 of 25
GDF Suez/RHPP - Ackerman, MS - 2010 Power MACT ICR

8/2/2010

Emissions Summary

Location: Common Stack - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 6.41E-03 7.28E-03 5.99E-03 0.007

ppm 6.81E+00 7.58E+00 6.24E+00 6.877

ppm@7%O2 5.95E+00 6.75E+00 5.56E+00 6.087

Location: Common Stack - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 1.12E-03 1.28E-03 1.36E-03 0.001

ppm 7.54E-01 8.49E-01 9.02E-01 0.835

ppm@7%O2 6.59E-01 7.56E-01 8.04E-01 0.740

Location: Common Stack - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.0018 0.00197 0.00199 0.002

lb/mmBtuO2 2.11E-07 2.28E-07 2.30E-07 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.00585 0.00672 0.00659 0.006

lb/mmBtuO2 6.86E-07 7.79E-07 7.63E-07 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.00107 0.0012 0.00133 0.001

lb/mmBtuO2 1.25E-07 1.39E-07 1.54E-07 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.00071 0.00058 0.00058 0.001

lb/mmBtuO2 8.33E-08 6.72E-08 6.72E-08 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.1337 0.0414 0.0381 0.071

lb/mmBtuO2 1.57E-05 4.80E-06 4.41E-06 0.000

Compound: Cobalt

Average

RunNumber 1 2 3

Thursday, February 10, 2011 Page 8 of 25
GDF Suez/RHPP - Ackerman, MS - 2010 Power MACT ICR

8/2/2010

Mass_mg 0.00491 0.00462 0.00433 0.005

lb/mmBtuO2 5.76E-07 5.35E-07 5.01E-07 0.000

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 135.8 121.2 141.2 132.733

lb/mmBtuO2 1.59E-02 1.40E-02 1.64E-02 0.015

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.07709 0.01148 0.00988 0.033

lb/mmBtuO2 9.04E-06 1.33E-06 1.14E-06 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.2177 0.2179 0.2873 0.241

lb/mmBtuO2 2.55E-05 2.53E-05 3.33E-05 0.000

Compound: Mercury

Average

RunNumber 1 2 3

Mass_mg 0.05126 0.12613 0.10086 0.093

lb/mmBtuO2 6.01E-06 1.46E-05 1.17E-05 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.0111 0.0099 0.0158 0.012

lb/mmBtuO2 1.30E-06 1.15E-06 1.83E-06 0.000

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.046 0.0119 0.0088 0.022

lb/mmBtuO2 5.40E-06 1.38E-06 1.02E-06 0.000

Location: Common Stack - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

lb/mmBtuO2 1.41E-01 1.19E-01 1.14E-01 0.125

ppm 6.56E+01 5.42E+01 5.21E+01 57.300

ppm@7%O2 5.73E+01 4.83E+01 4.64E+01 50.667

Location: Common Stack - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

lb/mmBtuO2 1.03E-01 1.09E-01 1.20E-01 0.111

ppm 6.64E+01 6.94E+01 7.62E+01 70.667

Thursday, February 10, 2011 Page 9 of 25
GDF Suez/RHPP - Ackerman, MS - 2010 Power MACT ICR

8/2/2010

Process Run Data

ppm@7%O2 5.80E+01 6.18E+01 6.79E+01 62.567

Location: Common Stack - OTM - 27/28

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 7.1 7.3 5.3 6.567

lb/mmBtuO2 1.55E-03 1.62E-03 1.21E-03 0.001

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 80.4 19.9 25.8 42.033

lb/mmBtuO2 1.75E-02 4.41E-03 5.91E-03 0.009

Thursday, February 10, 2011 Page 10 of 25
GDF Suez/RHPP - Ackerman, MS - 2010 Power MACT ICR

8/2/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Coal Firing Rate 478 tons/hr 5/18/10, 8:28 

AM - 11:45 

PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

3 Coal Firing Rate 482 tons/hr 5/18/10, 12:21 

PM - 3:34 

PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

4 Coal Firing Rate 480 tons/hr 5/18/10, 4:10 PM - 

7:23 PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

5 Coal Firing Rate 468 tons/hr 5/19/10, 9:11 

AM - 6:09 PM, 

Metals, PM

0

6 Coal Firing Rate 473 tons/hr 5/20/10, 7:14 

AM - 4:34 PM, 

Metals, PM

0

7 Coal Firing Rate 445 tons/hr 5/20-21/10, 7:30 

AM - 5:22 AM, 

Metals, PM

0

1 Steam Output 3384 1000 lbs/hr 5/18/10, 8:28 

AM - 11:45 

PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

3 Steam Output 3365 1000 lbs/hr 5/18/10, 12:21 

PM - 3:34 

PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

4 Steam Output 3421 1000 lbs/hr 5/18/10, 4:10 PM - 

7:23 PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

5 Steam Output 3311 1000 lbs/hr 5/19/10, 9:11 

AM - 6:09 PM, 

Metals, PM

0

Thursday, February 10, 2011 Page 11 of 25
GDF Suez/RHPP - Ackerman, MS - 2010 Power MACT ICR

8/2/2010

6 Steam Output 3387 1000 lbs/hr 5/20/10, 7:14 

AM - 4:34 PM, 

Metals, PM

0

7 Steam Output 3257 1000 lbs/hr 5/20-21/10, 7:30 

AM - 5:22 AM, 

Metals, PM

0

1 Average Heat Input 4946 MMBtu/hr 5/18/10, 8:28 

AM - 11:45 

PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

3 Average Heat Input 4960 MMBtu/hr 5/18/10, 12:21 

PM - 3:34 

PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

4 Average Heat Input 4694 MMBtu/hr 5/18/10, 4:10 PM - 

7:23 PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

5 Average Heat Input 4872 MMBtu/hr 5/19/10, 9:11 

AM - 6:09 PM, 

Metals, PM

0

6 Average Heat Input 4468 MMBtu/hr 5/20/10, 7:14 

AM - 4:34 PM, 

Metals, PM

0

7 Average Heat Input 4529 MMBtu/hr 5/20-21/10, 7:30 

AM - 5:22 AM, 

Metals, PM

0

1 Sorbent Type and Sorbent Injection Rate (if 

applicable)

4.84 tons/hr 5/18/10, 8:28 

AM - 11:45 

PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

3 Sorbent Type and Sorbent Injection Rate (if 

applicable)

5.77 tons/hr 5/18/10, 12:21 

PM - 3:34 

PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

4 Sorbent Type and Sorbent Injection Rate (if 

applicable)

5.53 tons/hr 5/18/10, 4:10 PM - 

7:23 PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

Thursday, February 10, 2011 Page 12 of 25
GDF Suez/RHPP - Ackerman, MS - 2010 Power MACT ICR

8/2/2010

5 Sorbent Type and Sorbent Injection Rate (if 

applicable)

5.89 tons/hr 5/19/10, 9:11 

AM - 6:09 PM, 

Metals, PM

0

6 Sorbent Type and Sorbent Injection Rate (if 

applicable)

6.81 tons/hr 5/20/10, 7:14 

AM - 4:34 PM, 

Metals, PM

0

7 Sorbent Type and Sorbent Injection Rate (if 

applicable)

3.97 tons/hr 5/20-21/10, 7:30 

AM - 5:22 AM, 

Metals, PM

0

1 Unit Net Electric Generation 431 MWh 5/18/10, 8:28 

AM - 11:45 

PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

3 Unit Net Electric Generation 432 MWh 5/18/10, 12:21 

PM - 3:34 

PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

4 Unit Net Electric Generation 433 MWh 5/18/10, 4:10 PM - 

7:23 PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

5 Unit Net Electric Generation 427 MWh 5/19/10, 9:11 

AM - 6:09 PM, 

Metals, PM

0

6 Unit Net Electric Generation 432 MWh 5/20/10, 7:14 

AM - 4:34 PM, 

Metals, PM

0

7 Unit Net Electric Generation 419 MWh 5/20-21/10, 7:30 

AM - 5:22 AM, 

Metals, PM

0

1 Flue Gas Oxygen Content 5 % 5/18/10, 8:28 

AM - 11:45 

PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

3 Flue Gas Oxygen Content 5.3 % 5/18/10, 12:21 

PM - 3:34 

PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

Thursday, February 10, 2011 Page 13 of 25
GDF Suez/RHPP - Ackerman, MS - 2010 Power MACT ICR

8/2/2010

4 Flue Gas Oxygen Content 5.3 % 5/18/10, 4:10 PM - 

7:23 PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

5 Flue Gas Oxygen Content 5.3 % 5/19/10, 9:11 

AM - 6:09 PM, 

Metals, PM

0

6 Flue Gas Oxygen Content 5.1 % 5/20/10, 7:14 

AM - 4:34 PM, 

Metals, PM

0

7 Flue Gas Oxygen Content 5.3 % 5/20-21/10, 7:30 

AM - 5:22 AM, 

Metals, PM

0

1 Flue Gas Carbon Dioxide Content 13.4 % 5/18/10, 8:28 

AM - 11:45 

PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

3 Flue Gas Carbon Dioxide Content 13.8 % 5/18/10, 12:21 

PM - 3:34 

PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

4 Flue Gas Carbon Dioxide Content 14.1 % 5/18/10, 4:10 PM - 

7:23 PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

5 Flue Gas Carbon Dioxide Content 13.8 % 5/19/10, 9:11 

AM - 6:09 PM, 

Metals, PM

0

6 Flue Gas Carbon Dioxide Content 13.7 % 5/20/10, 7:14 

AM - 4:34 PM, 

Metals, PM

0

7 Flue Gas Carbon Dioxide Content 13.8 % 5/20-21/10, 7:30 

AM - 5:22 AM, 

Metals, PM

0

1 Unit Gross Electric Output 492 MWh 5/18/10, 8:28 

AM - 11:45 

PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

Thursday, February 10, 2011 Page 14 of 25
GDF Suez/RHPP - Ackerman, MS - 2010 Power MACT ICR

8/2/2010

3 Unit Gross Electric Output 486 MWh 5/18/10, 12:21 

PM - 3:34 

PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

4 Unit Gross Electric Output 486 MWh 5/18/10, 4:10 PM - 

7:23 PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

5 Unit Gross Electric Output 482 MWh 5/19/10, 9:11 

AM - 6:09 PM, 

Metals, PM

0

6 Unit Gross Electric Output 484 MWh 5/20/10, 7:14 

AM - 4:34 PM, 

Metals, PM

0

7 Unit Gross Electric Output 476 MWh 5/20-21/10, 7:30 

AM - 5:22 AM, 

Metals, PM

0

1 Flue Gas Flow Rate 583495 dscfm 5/18/10, 8:28 

AM - 11:45 

PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

3 Flue Gas Flow Rate 585534 dscfm 5/18/10, 12:21 

PM - 3:34 

PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

4 Flue Gas Flow Rate 582393 dscfm 5/18/10, 4:10 PM - 

7:23 PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

5 Flue Gas Flow Rate 604108 dscfm 5/19/10, 9:11 

AM - 6:09 PM, 

Metals, PM

0

6 Flue Gas Flow Rate 599519 dscfm 5/20/10, 7:14 

AM - 4:34 PM, 

Metals, PM

0

7 Flue Gas Flow Rate 603297 dscfm 5/20-21/10, 7:30 

AM - 5:22 AM, 

Metals, PM

0

Thursday, February 10, 2011 Page 15 of 25
GDF Suez/RHPP - Ackerman, MS - 2010 Power MACT ICR

8/2/2010

1 Flue Gas Temperature 308 F 5/18/10, 8:28 

AM - 11:45 

PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

3 Flue Gas Temperature 312 F 5/18/10, 12:21 

PM - 3:34 

PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

4 Flue Gas Temperature 312 F 5/18/10, 4:10 PM - 

7:23 PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

5 Flue Gas Temperature 312 F 5/19/10, 9:11 

AM - 6:09 PM, 

Metals, PM

0

6 Flue Gas Temperature 305 F 5/20/10, 7:14 

AM - 4:34 PM, 

Metals, PM

0

7 Flue Gas Temperature 304 F 5/20-21/10, 7:30 

AM - 5:22 AM, 

Metals, PM

0

1 Flue Gas Moisture Content 19 % 5/18/10, 8:28 

AM - 11:45 

PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

3 Flue Gas Moisture Content 18.7 % 5/18/10, 12:21 

PM - 3:34 

PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

4 Flue Gas Moisture Content 19.1 % 5/18/10, 4:10 PM - 

7:23 PM,HCl, HF, 

HCN, CO, Nox, 

THC, Methane, 

HCOH

0

5 Flue Gas Moisture Content 18.7 % 5/19/10, 9:11 

AM - 6:09 PM, 

Metals, PM

0

6 Flue Gas Moisture Content 19.3 % 5/20/10, 7:14 

AM - 4:34 PM, 

Metals, PM

0

Thursday, February 10, 2011 Page 16 of 25
GDF Suez/RHPP - Ackerman, MS - 2010 Power MACT ICR

8/2/2010

APCD Run Data

Process Lab Run Data

7 Flue Gas Moisture Content 19.3 % 5/20-21/10, 7:30 

AM - 5:22 AM, 

Metals, PM

0

Run Name Value UOM Comments

Target

Value

1 BAGHOUSE 0 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value 0 Btu/lb

1 Fuel Moisture 0 %

1 Fuel Mercury Content 0 ppm

1 Fuel Cadmium Content 0 ppm

1 Ultimate/Proximate Analysis 0

1 Fuel Nickel Content 0 ppm

1 Fuel Arsenic Content 0 ppm

1 Fuel Chromium Content 0 ppm

1 Fuel Beryllium Content 0 ppm

1 Fuel Lead Content 0 ppm

1 Fuel Manganese 0 ppm

1 Fuel Chlorine Content 0 ppm

1 Fuel Fluorine Content 0 ppm

Thursday, February 10, 2011 Page 17 of 25
GDF Suez/RHPP - Ackerman, MS - 2010 Power MACT ICR

8/2/2010

Sampling / Stack Data Results Detail

Location Common Stack - 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

Thursday, February 10, 2011 Page 18 of 25
GDF Suez/RHPP - Ackerman, MS - 2010 Power MACT ICR

8/2/2010

Location Common Stack - 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

Thursday, February 10, 2011 Page 19 of 25
GDF Suez/RHPP - Ackerman, MS - 2010 Power MACT ICR

8/2/2010

Location Common Stack - Method 29

Average

Run Number 3 1 2

Test Date 5/21/2010 5/19/2010 5/20/2010

Run Start Time 7:30:00 AM 9:11:00 AM 7:14:00 AM

Run Finish Time 5:22:00 PM 6:09:00 PM 4:34:00 PM

Net Traversing Points 24 24 24

Net Run Time, minutes 420 420 420

Nozzle Diameter, inches 0.214 0.214 0.214 0.214

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.021 1.021 1.021 1.021

Barometric Pressure, inches of Mercury 29.53 29.55 29.47 29.517

Average Orifice Meter Differential, inches H2O 1.36 1.37 1.36 1.363

Dry Gas Meter Volume Sampled, cubic feet 250.875 252.050 248.890 250.605

Average Dry Gas Meter Temperature, °F 72.63 82.29 74.50 76.473

Dry Gas Meter Volume Sampled, dscf 251.456 248.307 248.090 249.284

Total Moisture Liquid collected, g 1273.7 1215.7 1263.4 1,250.933

Volume of Water Vapor, standard cubic feet 59.95 57.22 59.47 58.880

Moisture Content of Stack Gas, % 19.25 18.73 19.34 19.107

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

Dry Mole Fraction 0.8075 0.8127 0.8066 0.809

Carbon Dioxide, % 13.8 13.8 13.7 13.767

Oxygen, % 5.3 5.3 5.1 5.233

Carbon Monoxide & Nitrogen, % 80.9 80.9 81.2 81.000

Fuel Factor 1.13 1.13 1.15

Dry Molecular Weight, lb/lb-Mole 30.42 30.42 30.40 30.413

Wet Molecular weight, lb/lb-Mole 28.03 28.09 28.00 28.040

Flue Gas Static Pressure, inches of H2O -0.25 -0.25 -0.25 -0.250

Absolute Flue Gas Pressure, inches of Mercury 29.51 29.53 29.45 29.497

Average Stack Gas Temperature, °F 304.00 312.08 305.42 307.167

Average Velocity Head, inches of H2O 1.0819393441

1265

1.084035892

19294

1.073674229

41376

1.080

Average Stack Gas Velocity, feet/second 71.79 72.13 71.69 71.870

Stack Cross-Sectional Area, square feet 254.469 254.469 254.469 254.469

Dry Volumetric Flow Rate, dry scfm 603,310.4 604,095.8 599,460.8 602,289.000

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,096,099.8 1,101,290.9 1,094,573.0 1,097,321.2

33

Percent Isokinetic of Sampling Rate, % 101.1 99.7 100.4 100.400

Percent Excess Air, % 33.0 33.0 31.2 32.400

F-Factor, dscfm/MMBtu @ %O2 9860 9860 9860 9,860.000

Round Duct Diameter, inches 216 216 216

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 11950 11950 11950 11,950.000

Fc 1910 1910 1910 1,910.000

Thursday, February 10, 2011 Page 20 of 25
GDF Suez/RHPP - Ackerman, MS - 2010 Power MACT ICR

8/2/2010

Location Common Stack - 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

Thursday, February 10, 2011 Page 21 of 25
GDF Suez/RHPP - Ackerman, MS - 2010 Power MACT ICR

8/2/2010

Location Common Stack - 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

Thursday, February 10, 2011 Page 22 of 25
GDF Suez/RHPP - Ackerman, MS - 2010 Power MACT ICR

8/2/2010

Location Common Stack - 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

Thursday, February 10, 2011 Page 23 of 25
GDF Suez/RHPP - Ackerman, MS - 2010 Power MACT ICR

8/2/2010

Location Common Stack - 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

Thursday, February 10, 2011 Page 24 of 25
GDF Suez/RHPP - Ackerman, MS - 2010 Power MACT ICR

8/2/2010

Location Common Stack - 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

Thursday, February 10, 2011 Page 25 of 25