# EMISSIONS TEST REPORT

POLK POWER STATION FACILITY ID NUMBER: 1050233 EMISSION UNIT ID NO: -001 UNIT 1 SYNTHETIC GAS
VOLATILE ORGANIC COMPOUND S, SULFURIC ACID MIST, And OXIDES OF NITROGEN, SULF UR DIOXIDE FROM CEMS

January 15 & 16, 2009

Prepared For: Tampa Electric Company Polk Power Station P.O. Box 111 Tampa, Florida 33601-0111

Prepared By: Tampa Electric Company Environmental, Health, & Safety Air Services Group

Environmental, Health, & Safety Air Services Group 5010 Causeway Boulevard Tampa, Florida 33619- 6130

## REPORT CERTIFICATION
The sampling and subseque nt data entry/reduction detailed in this report was conducted at my direction, and I here by certify that this test report is authentic and accurate to the best of my knowledge.

Signature:__________________________ Jorge A. Varino Environmental Technician Test Team Lead Air Services Group Environmental Health & Safety Tampa Electric Company

I have reviewed the test performa nce, associated quality assurance activities, the resultant calculations, and the contents of this report, and certify that all project quality obj ectives have been met. Th is report is approved for submittal.

Signature:__________________________ Raymond A. McDarby, Jr. Senior Environmental Technician Quality Assurance/Quality Control Specialist Air Services Group Environmental Health & Safety Tampa Electric Company

I have reviewed the testing details and results submitted in this report, and hereby certify that this test report is authenti c and accurate to the best of my knowledge.

Signature:__________________________ David A. Smith, QSTI Coordinator – Air Services Group

Environmental Health & Safety Tampa Electric Company

## TABLE OF CONTENTS

SECTION PAGE NO. 1.0 INTRODUCTION 1 2.0 DISCUSSION OF RESULTS/EXECUTIVE SUMMARY 2 3.0 SOURCE DESCRIPTION/TEST PROCEDURES 4 4.0 TABULATED RESULTS VOLATILE ORGANIC COMPOUNDS DATA 7 SULFURIC ACID MIST TEST DATA 8 NITROGEN OXIDES & SULFUR DIOXIDE DATA FROM CEMS 9 HEAT INPUT CALCULATIONS, DECEMBER 15, 2008 10 HEAT INPUT CALCULATIONS, DECEMBER 16, 2008 11 5.0 STACK SAMPLING LOCATION DIAGRAM 13

APPENDICES A. VOLATILE ORGANIC COMPOUNDS TEST DATA FIELD DATA SHEETS LABORATORY ANALYSIS – ENTHALPY ANALYTICAL, INC. RM 25A DATA B. SULFURIC ACID MIST TEST DATA FIELD DATA SHEETS CALCULATED RUN DATA LABORATORY ANALYSIS EQUIPMENT CALIBRATIONS METHOD 8B DATA C. TURBINE DATA D. FUEL ANALYSIS E. CEMS DATA F. TEST PARTICIPANTS

### 1 

## 1.0 INTRODUCTION
On January 15 and 16, 2009, Tampa Electric Company’s, Environmental Services, Air Services Group performed source emission te sts, on Unit No. 1 at the Polk Power Station (PPS). The tests included Volatile Organic Compounds (VOCs) and Sulfuric Acid Mist (SAM). Unit No. 1 is a comb ined cycle combustion turbine generating unit. The combustion turbine was fired with syngas fr om the solid fuel gasification system. A blend of petroleum coke and bituminous coal wa s gasified for this test. Operations at PPS are authorized by the Flori da Department of Environmental Protection (FDEP) and permitted via Title V Permit No. 1050233-016-AV, Section III, sub-section A.

Nitrogen Oxides (NO x 

### ) and Sulfur Dioxide (SO 2 

### ) data was taken from the Continuous Emissions Monitoring System’s (CEMS) Da ta Acquisition and Handling System (DAHS) concurrent with the SAM testing, and is pr esented as averages over the test period.

In conjunction with the stack emissions test ing referenced above, additional source emissions testing was performed for SAM us ing method 8B as well as VOCs using Reference Method 25A. These efforts we re conducted to better correlate USEPA Reference Method results and plant operating process parameters.

### 2 

## 2.0 DISCUSSION OF RESULTS Executive Summary Tampa Electric Company Polk Power Station General Electric 7F Combined Cycle Combustion Turbine Emission Unit ID -001
Solid Fuel Derived Synthetic Gas Compliance Parameter Test Result FDEP Permit Limit VOC, lbs/hr 34 3 SAM, lbs/hr 47 55 January 15, 2009 NOX, lbs/hr 101.71 220.25 SO2, lbs/hr 344 357 Heat Input, mmBtu/hr 1633 -- Maximum Heat Input 1 1753 -- Unit Load (% of permit) 2 93% 90 – 100% January 16, 2009 NOX, lbs/hr 97.54 220.25 SO2, lbs/hr 302 357 Heat Input, mmBtu/hr 1622 Maximum Heat Input 1 1753 Unit Load (% of permit) 2 92% 90 – 100%
1 Maximum Heat Input is Permitted Maximum Heat Input Rate, 1755 mmBtu/hr @ 59o F, Corrected to Average Ambient Temperature Recorded During the Test Period.


### 2 Unit Load (% of permit) is Heat Input Divided by Maximum Heat Input times 100. 

### The Volatile Organic Compounds (VOCs) emi ssion rate was derived from three 1-hour Reference Method 18 test runs conduct ed on January 15, 2009. The calculated average VOCs emission rate was 34 lbs/hr. The FDEP permitted emission rate is 3 lbs/hr based on a 30-day rolling average.

The Sulfuric Acid Mist (SAM) emission ra te was derived from six 1-hour Reference Method 8 test runs conducted on January 15 and 16, 2009. T he calculated average SAM emission rate was 47 lbs/hr. Run num ber 2 was not included in the test average when it failed the Chauvenet’s Cr iteria statistical test for outliers. The FDEP permitted emission rate is 55 lbs/hr based on a 30-day rolling average.

### 3 

### During the SAM testing, the Nitrogen Oxides (NO x 

### ) average emission rate was 99.62 lbs/hr.

During the SAM testing, the Sulfur Dioxide (SO 2 

### ) average emission rate was 323 lbs/hr.

During the January 15 th 

### , test Unit No. 1 was operated at an average heat input of 1633 mmBtu/hr. The FDEP permitted heat i nput is 1755 mmBtu/hr, at an ambient temperature of 59o (corrected to 1753 mmBtu/hr based on an average inlet vane temperature of 67o F, and the manufacturer’s heat input correction curve for this unit). The unit operated at 93% of permitted capacity.

During the January 16 th 

### , test Unit No. 1 was operated at an average heat input of 1622 mmBtu/hr. The FDEP permitted heat i nput is 1755 mmBtu/hr, at an ambient temperature of 59o (corrected to 1753 mmBtu/hr based on an average inlet vane temperature of 63o F, and the manufacturer’s heat input correction curve for this unit). The unit operated at 92% of permitted capacity.

### 4 

## 3.0 SOURCE DESCRIPTION/TEST PROCEDURES

Polk Power Electrical Generat ing Station is located at County Road 630 approximately 13 miles southwest of Bartow, Polk County, Florida. Unit No. 1 is a Combined Cycle Combustion Turbine generating unit, with a net capacity of 192 MW when fired with Syngas fuel. The source sampling location c onsists of a circular stack 19 feet in diameter with four sample ports located 90 degrees apart on the stack circumference. A diagram of the stack sampling locati on is included along with other pertinent information on the test site.

Volatile Organic Compound sampling wa s performed in accordance with USEPA Reference Method 18 “Measurement of Ga seous Organic Compound Emissions by Gas Chromatography”. Analysis was performed by Enthalpy Analytical, Inc. The analysis detected Isopropyl Alcohol (IPA) contamination in bag samp les 1 and 2. The IPA was “backed out” of the analysis. The samples we re used in the calculation of the average, but are considered to be suspect.

Sulfuric Acid Mist sampling was perfo rmed in accordance with USEPA Reference Method 8 “Determination of Sulfuric Acid Mist and Sulfur Dioxide Emissions From Stationary Sources”. Seven, one-hour runs were conducted for this test. Run number 1 was excluded from the averagi ng due to reagent carry over after the post-test leak check. Run number 2 was excluded from the averaging when it failed a routine Chauvenet’s Criteria statistical test for out liers during the quality assurance phase of the post test activities. All data is presented in the Appendices for review. During the compliance test, Method 8B “Determination of Sulfur Oxides Includi ng Sulfur Dioxide, Sulfur Trioxide, and Sulfuric Acid Vapor and Mist From Stationary Sources Using a Controlled Condensation Sampling Apparatus” we re performed as part of an alternative method validation test. This data is al so included in the Appendices for review.

Sulfur Dioxide and Nitrogen Oxides emissions data were taken from the CEMS DAHS. This data was taken as 1-minute averages ov er the time frame consistent with the Sulfuric Acid Mist testing.

### 5 

### Plant operational data was taken from the Pl ant Information (PI) se rver system. Data captured included the minute average load, minute fuel flow, minute inlet vane temperature, and minute saturator readings.

### 6 

## 4.0 TABULATED RESULTS

## POLK POWER STATION V

OLATILE ORGANIC COMPOUNDS DAT A

THC, ppm VOC 

### Flow Rate VOC Run # Start Stop as C 6 

### H 14 

### lb/scf scf/hr lbs/hr 1 12:05 13:05 1.71 3.826E-07 4.787E+07 18 2 13:08 14:13 7.92 1.772E-06 4.759E+07 84 3 14:29 15:15 0.00 0.000E+00 4.787E+07 0 Averages: 34

VOC, lb/scf calculated as: ppm VOC x C f 

### where: C f



### = Mole wieght of hexane (86.18 lb/lb-mole) x 10 - 6 

### / (385.15 scf/lb-mole) 2.238E-07 lbs/dscf

VOC, lbs/hr calculated as: VOC, lb/scf x Stack Flow, scf/hr

Notation to Data: Runs 1 and 2 were compromised by IPA in the samples. The IPA component were "backed out" of the analysis, the resultant included in this data analysis. Run 3 was reported as ND (non-detect) for organic compunds. Test Times 

### COMBINED CYCLE COMBUSTION TURBINE UNIT 1 January 15, 2009

7Environmental ServicesAir Services Group40 CFR 60, Appendix A - Test MethodsReference Method 8Test SummaryCustomer: Polk Power StationFacility: Unit 1Sampling Location:StackOperating Conditions:Full LoadTest Date:Run #2Run #3Run #4Run #5Run #6Run #7AverageGas Flow RatesQs, acfm:1360657.3 1368571.0 1376586.5 1373822.1 1373886.0 1369871.2 1370565.7Qs(std), dscfm:875853.1 882161.3 881473.8 891026.7 888880.3 886364.2 884293.2Sampled Volume, Vm(std), dscf:39.62 39.86 40.04 39.83 39.92 39.6639.823Stack Moisture, Bwsx 100, %:5.064.92 5.38 4.60 4.74 4.724.903Isokinetic Sampling Rate, I,%: 101100.9 101.4 99.8 100.3 99.9100.55CH2SO4,lb/dscf:2.108E-06 1.089E-06 7.952E-07 6.848E-07 7.991E-07 1.089E-06 1.095E-06EH2SO4, lb/mmBtu:0.0541 0.0280 0.0204 0.0176 0.0205 0.02800.0281EH2SO4, lbs/hr:111584237435858Average adjusted for outlier:47January 15, 2009January 16, 2009Sulfuric Acid Mist - Reference Method 8Notation to Data:Run #1 was excluded due to reagent carry over after the postrun leak check. Run #2 should be excluded due to failedChauvenet’s Criteria outlier test. All data is available in appendices for review.8

## POLK POWER STATIO N N O X 

## & S O 2 

## COMPLIANCE DATA FROM CEM S

NO x 

### SO 2 

### Flow NO x 

### SO 2 

### ppmvw ppmvw kscfmw lbs/hr lbs/hr

17.85 43.37 795.41 101.71 344

NO x 

### SO 2 

### Flow NO x 

### SO 2 

### ppmvw ppmvw kscfmw lbs/hr lbs/hr

17.23 38.41 790.11 97.54 302
NOX, lbs/hr calculated as: NOX, ppmvw x 1.194E-07 x Flow, kscfmw x 60 min/hr x 1000/ k
SO2, lbs/hr calculated as: SO2, ppmvw x 1.660E-07 x Flow, kscfmw x 60 min/hr x 1000/ k 

### January 16, 2009

CEM Data Calculated Data

HEAT RECOVERY STEAM GENERATO R UNIT 1 January 15, 2009

CEM Data Calculated Data

9

## POLK POWER STATIO N HEAT INPUT CALCULATIO N

Average fuel flow: 6548.709 Kcfh Mole weight correction to meter cal: 0.9883 mole weight correction factor Corrected fuel flow:1 6472.0891 Kcfh, corrected for density Average moisture: 2.7 % H 2 

### 0 added to fuel Corrected fuel flow:2 6296.7362 Kscfh, corrected for moisture Gross heating value of fuel (HHV): 259.30 Btu/scf Heat Input: 1633 mmBtu/hr
Average fuel flow from Plant Information Data Base. Mole weight correction factor to meter calibration is taken from ratio of syngas mole weight to calibration gas mole weight. 1Average fuel flow times mole weight correction factor. 2Corrected fuel flow times (1 - (Average moisture / 100)). Gross Heating value of fuel (HHV) is from fuel analysis. Heat input is (HHV x Co rrected fuel flow) / 1000. 

### COMBINED CYCLE COMBUSTION TURBINE UNIT 1 January 15, 2009

10

## POLK POWER STATIO N HEAT INPUT CALCULATIO N

Average fuel flow: 6602.319 Kcfh Mole weight correction to meter cal: 0.9883 mole weight correction factor Corrected fuel flow:1 6525.0719 Kcfh, corrected for density Average moisture: 2.9 % H 2 

### 0 added to fuel Corrected fuel flow:2 6335.8448 Kscfh, corrected for moisture Gross heating value of fuel (HHV): 255.93 Btu/scf Heat Input: 1622 mmBtu/hr
Average fuel flow from Plant Information Data Base. Mole weight correction factor to meter calibration is taken from ratio of syngas mole weight to calibration gas mole weight. 1Average fuel flow times mole weight correction factor. 2Corrected fuel flow times (1 - (Average moisture / 100)). Gross Heating value of fuel (HHV) is from fuel analysis. Heat input is (HHV x Co rrected fuel flow) / 1000. 

### UNIT 1 January 16, 2009 COMBINED CYCLE COMBUSTION TURBINE

11

### 12 

## 5.0 SAMPLING LOCATION DIAGRAM

### 13 UNFIRED HEAT

RECOVERY BOILER TRANSITION
DUCT

EXHAUST FROM TURBINE 14 FT.

38 FT. 150 FT.

136 FT. 

## POLK POWER STATION COMBUSTION TURBINE COMBINED CYCLE UNIT NO.1 TEST LOCATION

PORT LOCATION PLAN 19.0 FT.ID.

STACK DIAMETERS DOWNSTREAM FROM DISTURBANCE = 2.0 STACK DIAMETERS UPSTREAM FROM DISTURBANCE = 0.7 STACK DIAMETER = 19.0 FT. STACK AREA = 283.529 S Q . FT. STACK AREA =40828.138 SQ. IN.

## APPENDIX A

VOLATILE ORGANIC COMPOUNDS DATA

### FIELD DATA SHEETS

### LABORATORY ANALYSIS – ENTHALPY ANALYTICAL, INC

### RM 25A DATAPPS - HRSG RM25A Engineering Data Polk Unit 1 Compliance - Report RUN 1 01/15/2009
Analyzer Calibration Error (Eq 7E-1) oTHCB Analyzer Range 10 Units PPM Low Level Certified Value (PPM or %) 3.094 Mid Level Certified Value (PPM or %) 4.959 High Level Certified Value (PPM or %) 8.575 Zero Level Observed -0.011 Low Level Observed 3.066 Mid Level Observed 4.835 High Level Observed 8.61 Zero Calibration Error ACE -0.13 Low Level Calibration Error ACE -0.33 Mid Level Calibration Error ACE -1.45 High Level Calibration Error ACE 0.41 Initial Readings Zero -0.018 Span 8.61 Final Readings Zero 0.051 Span 8.462
System Bias (Eq 7E-2) Initial Zero Bias SB -0.08 Initial Span Bias SB 0 Final Zero Bias SB 0.72 Final Span Bias SB -1.73
System Calibration Error (Eq 7E-3) Initial Zero SCE -0.21 Initial Span SCE 0.41 Final Zero SCE 0.59 Final Span SCE -1.32
Drift Assessment (Eq 7E-4) Zero Drift D 0.8 Span Drift D 1.73
Effluent Gas Concentration (Eq 7E-5) Raw Results -0.44 Corrected Results (ppmv) -0.46

Page 1 of 3PPS - HRSG RM25A Engineering Data Polk Unit 1 Compliance - Report RUN 2 01/15/2009
Analyzer Calibration Error (Eq 7E-1) oTHCB Analyzer Range 10 Units PPM Low Level Certified Value (PPM or %) 3.094 Mid Level Certified Value (PPM or %) 4.959 High Level Certified Value (PPM or %) 8.575 Zero Level Observed -0.011 Low Level Observed 3.066 Mid Level Observed 4.835 High Level Observed 8.61 Zero Calibration Error ACE -0.13 Low Level Calibration Error ACE -0.33 Mid Level Calibration Error ACE -1.45 High Level Calibration Error ACE 0.41 Initial Readings Zero 0.051 Span 8.462 Final Readings Zero -0.099 Span 8.365
System Bias (Eq 7E-2) Initial Zero Bias SB 0.72 Initial Span Bias SB -1.73 Final Zero Bias SB -1.03 Final Span Bias SB -2.86
System Calibration Error (Eq 7E-3) Initial Zero SCE 0.59 Initial Span SCE -1.32 Final Zero SCE -1.15 Final Span SCE -2.45
Drift Assessment (Eq 7E-4) Zero Drift D 1.75 Span Drift D 1.13
Effluent Gas Concentration (Eq 7E-5) Raw Results -0.45 Corrected Results (ppmv) -0.43

Page 2 of 3PPS - HRSG RM25A Engineering Data Polk Unit 1 Compliance - Report RUN 3 01/15/2009
Analyzer Calibration Error (Eq 7E-1) oTHCB Analyzer Range 10 Units PPM Low Level Certified Value (PPM or %) 3.094 Mid Level Certified Value (PPM or %) 4.959 High Level Certified Value (PPM or %) 8.575 Zero Level Observed -0.011 Low Level Observed 3.066 Mid Level Observed 4.835 High Level Observed 8.61 Zero Calibration Error ACE -0.13 Low Level Calibration Error ACE -0.33 Mid Level Calibration Error ACE -1.45 High Level Calibration Error ACE 0.41 Initial Readings Zero -0.099 Span 8.365 Final Readings Zero -0.065 Span 8.438
System Bias (Eq 7E-2) Initial Zero Bias SB -1.03 Initial Span Bias SB -2.86 Final Zero Bias SB -0.63 Final Span Bias SB -2.01
System Calibration Error (Eq 7E-3) Initial Zero SCE -1.15 Initial Span SCE -2.45 Final Zero SCE -0.76 Final Span SCE -1.6
Drift Assessment (Eq 7E-4) Zero Drift D 0.4 Span Drift D 0.85
Effluent Gas Concentration (Eq 7E-5) Raw Results -0.59 Corrected Results (ppmv) -0.51

Page 3 of 3

## APPENDIX B
SULFURIC ACID MIST TEST DATA

### FIELD DATA SHEETS

### CALCULATED RUN DATAEnvironmental Services A ir Services Group

40 CFR 60, Appendix A - Test Methods Reference Method 8

Test Calculations

Customer: Polk Power Station Facility: Unit 1 Sampling Location: Stack Operating Conditions: Full Load Run Number: 1 Date: 01/15/2009
Sample Time, θ : 60 minutes Nozzle Diameter, D n : 0.197 inches Barometric Pressure, P b : 30.10 "Hg Nozzle Area, A n : 0.00021166 ft 2 Stack Pressure, P s : 30.04 "Hg Average Orifice Meter, Δ H: 1.370 "H 2 O Effective Stack Area, A s : 283.529 ft 2 Sample Volume, V m : 39.978 ft 3 Pitot Coefficient, Cp: 0.84 dimensionless Average Meter Temp., T m : 62.3 o F Gas Analysis: 9.0 % CO 2 Average Stack Temp., T s : 321.8 o F 12.0 % O 2 Average √ Δ p: 1.186 "H 2 O

0.0 % CO Condensate Volume, V lc : 8.9 ml 79.0 % N 2 Meter Box Y: 0.974 dimensionless

Data Calculated from Source Measurements: V w(std) = 4.714E-02 x V lc 0.420 scf V m(std) = 17.647 x V m x Y x (P b + ( Δ H / 13.6)) / (T m +460) 39.733 dscf B ws = V w(std) / (V m(std) + V w(std) ) 0.010 % FDA = 1.0 - B ws 0.990 % M d = (0.44 x %CO 2 ) + (0.32 x %O 2 ) + (0.28 x (%N 2 + % CO)) 29.92 lb./lb. mole M s = (M d x FDA) + (18.0 x B ws ) 29.80 lb./lb. mole

v s = 85.49 x C p x ( √Δ p) x ( √ (T s + 460) / (M s x P s )) 79.58 ft/second Q s = v s x A s x 60 1353724.5 acf/minute Q s(std) = Q s x FDA x (528 / (T s + 460)) x (P s / 29.92)) 908441.2 dscf/minute I = (T s + 460) x ((2.67E-03 x V lc ) + (V m(std) / 17.647)) x 100 / ( θ x P s x A n x v s x 60 97.6 %

Data from Laboratory Analysis: H 2 SO 4 Normality of Barium Chloride titrant, N 0.0103 Volume Titrant Blank, V tb 0.02 Volume Titrant Sample, V t 2.7 Volume of Sample Aliquot, V a 10 Total Volume of Solution, V soln 500

Calculated Concentration and Emission Rate Data:

C H2SO4 = 1.081E-04 x (N x (V t - V tb ) x (V soln / V a )) / V m(std) = 3.755E-06 lb/dscf F c -factor = 2310 dscf/mmBtu E H2SO4 = C H2SO4 x F c -factor x (100/%CO 2 ) = 0.09638 lb/mmBtu E H2SO4 = C H2SO4 x Q s(std) x 60 = 205 lb/hrEnvironmental Services A ir Services Group

40 CFR 60, Appendix A - Test Methods Reference Method 8

Test Calculations

Customer: Polk Power Station Facility: Unit 1 Sampling Location: Stack Operating Conditions: Full Load Run Number: 2 Date: 01/15/2009
Sample Time, θ : 60 minutes Nozzle Diameter, D n : 0.197 inches Barometric Pressure, P b : 30.10 "Hg Nozzle Area, A n : 0.00021166 ft 2 Stack Pressure, P s : 30.05 "Hg Average Orifice Meter, Δ H: 1.382 "H 2 O Effective Stack Area, A s : 283.529 ft 2 Sample Volume, V m : 40.455 ft 3 Pitot Coefficient, Cp: 0.84 dimensionless Average Meter Temp., T m : 70.0 o F Gas Analysis: 9.0 % CO 2 Average Stack Temp., T s : 322.0 o F 12.0 % O 2 Average √ Δ p: 1.182 "H 2 O

0.0 % CO Condensate Volume, V lc : 44.8 ml 79.0 % N 2 Meter Box Y: 0.974 dimensionless

Data Calculated from Source Measurements: V w(std) = 4.714E-02 x V lc 2.112 scf V m(std) = 17.647 x V m x Y x (P b + ( Δ H / 13.6)) / (T m +460) 39.624 dscf B ws = V w(std) / (V m(std) + V w(std) ) 0.051 % FDA = 1.0 - B ws 0.949 % M d = (0.44 x %CO 2 ) + (0.32 x %O 2 ) + (0.28 x (%N 2 + % CO)) 29.92 lb./lb. mole M s = (M d x FDA) + (18.0 x B ws ) 29.32 lb./lb. mole

v s = 85.49 x C p x ( √Δ p) x ( √ (T s + 460) / (M s x P s )) 79.98 ft/second Q s = v s x A s x 60 1360657.3 acf/minute Q s(std) = Q s x FDA x (528 / (T s + 460)) x (P s / 29.92)) 875853.1 dscf/minute I = (T s + 460) x ((2.67E-03 x V lc ) + (V m(std) / 17.647)) x 100 / ( θ x P s x A n x 101.0 %

Data from Laboratory Analysis: H 2 SO 4 Normality of Barium Chloride titrant, N 0.0103 Volume Titrant Blank, V tb 0.02 Volume Titrant Sample, V t 1.52 Volume of Sample Aliquot, V a 10 Total Volume of Solution, V soln 500

Calculated Concentration and Emission Rate Data:

C H2SO4 = 1.081E-04 x (N x (V t - V tb ) x (V soln / V a )) / V m(std) = 2.108E-06 lb/dscf F c -factor = 2310 dscf/MMBtu E H2SO4 = C H2SO4 x F c -factor x (100/%CO 2 ) = 0.05409 lb/MMBtu E H2SO4 = C H2SO4 x Q s(std) x 60 = 111 lb/hrEnvironmental Services A ir Services Group

40 CFR 60, Appendix A - Test Methods Reference Method 8

Test Calculations

Customer: Polk Power Station Facility: Unit 1 Sampling Location: Stack Operating Conditions: Full Load Run Number: 3 Date: 01/15/2009
Sample Time, θ : 60 minutes Nozzle Diameter, D n : 0.197 inches Barometric Pressure, P b : 30.10 "Hg Nozzle Area, A n : 0.00021166 ft 2 Stack Pressure, P s : 30.04 "Hg Average Orifice Meter, Δ H: 1.407 "H 2 O Effective Stack Area, A s : 283.529 ft 2 Sample Volume, V m : 40.955 ft 3 Pitot Coefficient, Cp: 0.84 dimensionless Average Meter Temp., T m : 73.4 o F Gas Analysis: 9.0 % CO 2 Average Stack Temp., T s : 322.0 o F 12.0 % O 2 Average √ Δ p: 1.189 "H 2 O

0.0 % CO Condensate Volume, V lc : 43.8 ml 79.0 % N 2 Meter Box Y: 0.974 dimensionless

Data Calculated from Source Measurements: V w(std) = 4.714E-02 x V lc 2.065 scf V m(std) = 17.647 x V m x Y x (P b + ( Δ H / 13.6)) / (T m +460) 39.862 dscf B ws = V w(std) / (V m(std) + V w(std) ) 0.049 % FDA = 1.0 - B ws 0.951 % M d = (0.44 x %CO 2 ) + (0.32 x %O 2 ) + (0.28 x (%N 2 + % CO)) 29.92 lb./lb. mole M s = (M d x FDA) + (18.0 x B ws ) 29.33 lb./lb. mole

v s = 85.49 x C p x ( √Δ p) x ( √ (T s + 460) / (M s x P s )) 80.45 ft/second Q s = v s x A s x 60 1368571.0 acf/minute Q s(std) = Q s x FDA x (528 / (T s + 460)) x (P s / 29.92)) 882161.3 dscf/minute I = (T s + 460) x ((2.67E-03 x V lc ) + (V m(std) / 17.647)) x 100 / ( θ x P s x A n x 100.9 %

Data from Laboratory Analysis: H 2 SO 4 Normality of Barium Chloride titrant, N 0.0103 Volume Titrant Blank, V tb 0.02 Volume Titrant Sample, V t 0.8 Volume of Sample Aliquot, V a 10 Total Volume of Solution, V soln 500

Calculated Concentration and Emission Rate Data:

C H2SO4 = 1.081E-04 x (N x (V t - V tb ) x (V soln / V a )) / V m(std) = 1.089E-06 lb/dscf F c -factor = 2310 dscf/MMBtu E H2SO4 = C H2SO4 x F c -factor x (100/%CO 2 ) = 0.02796 lb/MMBtu E H2SO4 = C H2SO4 x Q s(std) x 60 = 58 lb/hrEnvironmental Services A ir Services Group

40 CFR 60, Appendix A - Test Methods Reference Method 8

Test Calculations

Customer: Polk Power Station Facility: Unit 1 Sampling Location: Stack Operating Conditions: Full Load Run Number: 4 Date: 01/15/2009
Sample Time, θ : 60 minutes Nozzle Diameter, D n : 0.197 inches Barometric Pressure, P b : 30.05 "Hg Nozzle Area, A n : 0.00021166 ft 2 Stack Pressure, P s : 29.99 "Hg Average Orifice Meter, Δ H: 1.423 "H 2 O Effective Stack Area, A s : 283.529 ft 2 Sample Volume, V m : 41.111 ft 3 Pitot Coefficient, Cp: 0.84 dimensionless Average Meter Temp., T m : 72.1 o F Gas Analysis: 9.0 % CO 2 Average Stack Temp., T s : 322.1 o F 16.0 % O 2 Average √ Δ p: 1.197 "H 2 O

0.0 % CO Condensate Volume, V lc : 48.3 ml 75.0 % N 2 Meter Box Y: 0.974 dimensionless

Data Calculated from Source Measurements: V w(std) = 4.714E-02 x V lc 2.277 scf V m(std) = 17.647 x V m x Y x (P b + ( Δ H / 13.6)) / (T m +460) 40.043 dscf B ws = V w(std) / (V m(std) + V w(std) ) 0.054 % FDA = 1.0 - B ws 0.946 % M d = (0.44 x %CO 2 ) + (0.32 x %O 2 ) + (0.28 x (%N 2 + % CO)) 30.08 lb./lb. mole M s = (M d x FDA) + (18.0 x B ws ) 29.43 lb./lb. mole

v s = 85.49 x C p x ( √Δ p) x ( √ (T s + 460) / (M s x P s )) 80.92 ft/second Q s = v s x A s x 60 1376586.5 acf/minute Q s(std) = Q s x FDA x (528 / (T s + 460)) x (P s / 29.92)) 881473.8 dscf/minute I = (T s + 460) x ((2.67E-03 x V lc ) + (V m(std) / 17.647)) x 100 / ( θ x P s x A n x v s 101.4 %

Data from Laboratory Analysis: H 2 SO 4 Normality of Barium Chloride titrant, N 0.0103 Volume Titrant Blank, V tb 0.02 Volume Titrant Sample, V t 2.88 Volume of Sample Aliquot, V a 50 Total Volume of Solution, V soln 500

Calculated Concentration and Emission Rate Data:

C H2SO4 = 1.081E-04 x (N x (V t - V tb ) x (V soln / V a )) / V m(std) = 7.952E-07 lb/dscf F c -factor = 2310 dscf/MMBtu E H2SO4 = C H2SO4 x F c -factor x (100/%CO 2 ) = 0.02041 lb/MMBtu E H2SO4 = C H2SO4 x Q s(std) x 60 = 42 lb/hrEnvironmental Services A ir Services Group

40 CFR 60, Appendix A - Test Methods Reference Method 8

Test Calculations

Customer: Polk Power Station Facility: Unit 1 Sampling Location: Stack Operating Conditions: Full Load Run Number: 5 Date: 01/15/2009
Sample Time, θ : 60 minutes Nozzle Diameter, D n : 0.197 inches Barometric Pressure, P b : 30.18 "Hg Nozzle Area, A n : 0.00021166 ft 2 Stack Pressure, P s : 30.12 "Hg Average Orifice Meter, Δ H: 1.390 "H 2 O Effective Stack Area, A s : 283.529 ft 2 Sample Volume, V m : 39.852 ft 3 Pitot Coefficient, Cp: 0.84 dimensionless Average Meter Temp., T m : 60.8 o F Gas Analysis: 9.0 % CO 2 Average Stack Temp., T s : 322.0 o F 12.0 % O 2 Average √ Δ p: 1.196 "H 2 O

0.0 % CO Condensate Volume, V lc : 40.7 ml 79.0 % N 2 Meter Box Y: 0.974 dimensionless

Data Calculated from Source Measurements: V w(std) = 4.714E-02 x V lc 1.919 scf V m(std) = 17.647 x V m x Y x (P b + ( Δ H / 13.6)) / (T m +460) 39.833 dscf B ws = V w(std) / (V m(std) + V w(std) ) 0.046 % FDA = 1.0 - B ws 0.954 % M d = (0.44 x %CO 2 ) + (0.32 x %O 2 ) + (0.28 x (%N 2 + % CO)) 29.92 lb./lb. mole M s = (M d x FDA) + (18.0 x B ws ) 29.37 lb./lb. mole

v s = 85.49 x C p x ( √Δ p) x ( √ (T s + 460) / (M s x P s )) 80.76 ft/second Q s = v s x A s x 60 1373822.1 acf/minute Q s(std) = Q s x FDA x (528 / (T s + 460)) x (P s / 29.92)) 891026.7 dscf/minute I = (T s + 460) x ((2.67E-03 x V lc ) + (V m(std) / 17.647)) x 100 / ( θ x P s x A n x v s 99.8 %

Data from Laboratory Analysis: H 2 SO 4 Normality of Barium Chloride titrant, N 0.0103 Volume Titrant Blank, V tb 0.02 Volume Titrant Sample, V t 4.92 Volume of Sample Aliquot, V a 100 Total Volume of Solution, V soln 500

Calculated Concentration and Emission Rate Data:

C H2SO4 = 1.081E-04 x (N x (V t - V tb ) x (V soln / V a )) / V m(std) = 6.848E-07 lb/dscf F c -factor = 2310 dscf/MMBtu E H2SO4 = C H2SO4 x F c -factor x (100/%CO 2 ) = 0.01758 lb/MMBtu E H2SO4 = C H2SO4 x Q s(std) x 60 = 37 lb/hrEnvironmental Services A ir Services Group

40 CFR 60, Appendix A - Test Methods Reference Method 8

Test Calculations

Customer: Polk Power Station Facility: Unit 1 Sampling Location: Stack Operating Conditions: Full Load Run Number: 3 Date: 01/15/2009
Sample Time, θ : 60 minutes Nozzle Diameter, D n : 0.197 inches Barometric Pressure, P b : 30.15 "Hg Nozzle Area, A n : 0.00021166 ft 2 Stack Pressure, P s : 30.10 "Hg Average Orifice Meter, Δ H: 1.404 "H 2 O Effective Stack Area, A s : 283.529 ft 2 Sample Volume, V m : 40.427 ft 3 Pitot Coefficient, Cp: 0.84 dimensionless Average Meter Temp., T m : 66.6 o F Gas Analysis: 9.0 % CO 2 Average Stack Temp., T s : 322.1 o F 12.0 % O 2 Average √ Δ p: 1.195 "H 2 O

0.0 % CO Condensate Volume, V lc : 42.1 ml 79.0 % N 2 Meter Box Y: 0.974 dimensionless

Data Calculated from Source Measurements: V w(std) = 4.714E-02 x V lc 1.985 scf V m(std) = 17.647 x V m x Y x (P b + ( Δ H / 13.6)) / (T m +460) 39.918 dscf B ws = V w(std) / (V m(std) + V w(std) ) 0.047 % FDA = 1.0 - B ws 0.953 % M d = (0.44 x %CO 2 ) + (0.32 x %O 2 ) + (0.28 x (%N 2 + % CO)) 29.92 lb./lb. mole M s = (M d x FDA) + (18.0 x B ws ) 29.36 lb./lb. mole

v s = 85.49 x C p x ( √Δ p) x ( √ (T s + 460) / (M s x P s )) 80.76 ft/second Q s = v s x A s x 60 1373886.0 acf/minute Q s(std) = Q s x FDA x (528 / (T s + 460)) x (P s / 29.92)) 888880.3 dscf/minute I = (T s + 460) x ((2.67E-03 x V lc ) + (V m(std) / 17.647)) x 100 / ( θ x P s x A n x v s 100.3 %

Data from Laboratory Analysis: H 2 SO 4 Normality of Barium Chloride titrant, N 0.0103 Volume Titrant Blank, V tb 0.02 Volume Titrant Sample, V t 5.75 Volume of Sample Aliquot, V a 100 Total Volume of Solution, V soln 500

Calculated Concentration and Emission Rate Data:

C H2SO4 = 1.081E-04 x (N x (V t - V tb ) x (V soln / V a )) / V m(std) = 7.991E-07 lb/dscf F c -factor = 2310 dscf/MMBtu E H2SO4 = C H2SO4 x F c -factor x (100/%CO 2 ) = 0.02051 lb/MMBtu E H2SO4 = C H2SO4 x Q s(std) x 60 = 43 lb/hrEnvironmental Services A ir Services Group

40 CFR 60, Appendix A - Test Methods Reference Method 8

Test Calculations

Customer: Polk Power Station Facility: Unit 1 Sampling Location: Stack Operating Conditions: Full Load Run Number: 7 Date: 01/15/2009
Sample Time, θ : 60 minutes Nozzle Diameter, D n : 0.197 inches Barometric Pressure, P b : 30.15 "Hg Nozzle Area, A n : 0.00021166 ft 2 Stack Pressure, P s : 30.10 "Hg Average Orifice Meter, Δ H: 1.396 "H 2 O Effective Stack Area, A s : 283.529 ft 2 Sample Volume, V m : 40.189 ft 3 Pitot Coefficient, Cp: 0.84 dimensionless Average Meter Temp., T m : 66.9 o F Gas Analysis: 9.0 % CO 2 Average Stack Temp., T s : 322.1 o F 12.0 % O 2 Average √ Δ p: 1.192 "H 2 O

0.0 % CO Condensate Volume, V lc : 41.7 ml 79.0 % N 2 Meter Box Y: 0.974 dimensionless

Data Calculated from Source Measurements: V w(std) = 4.714E-02 x V lc 1.966 scf V m(std) = 17.647 x V m x Y x (P b + ( Δ H / 13.6)) / (T m +460) 39.661 dscf B ws = V w(std) / (V m(std) + V w(std) ) 0.047 % FDA = 1.0 - B ws 0.953 % M d = (0.44 x %CO 2 ) + (0.32 x %O 2 ) + (0.28 x (%N 2 + % CO)) 29.92 lb./lb. mole M s = (M d x FDA) + (18.0 x B ws ) 29.36 lb./lb. mole

v s = 85.49 x C p x ( √Δ p) x ( √ (T s + 460) / (M s x P s )) 80.53 ft/second Q s = v s x A s x 60 1369871.2 acf/minute Q s(std) = Q s x FDA x (528 / (T s + 460)) x (P s / 29.92)) 886364.2 dscf/minute I = (T s + 460) x ((2.67E-03 x V lc ) + (V m(std) / 17.647)) x 100 / ( θ x P s x A n x v s 99.9 %

Data from Laboratory Analysis: H 2 SO 4 Normality of Barium Chloride titrant, N 0.0103 Volume Titrant Blank, V tb 0.02 Volume Titrant Sample, V t 7.78 Volume of Sample Aliquot, V a 100 Total Volume of Solution, V soln 500

Calculated Concentration and Emission Rate Data:

C H2SO4 = 1.081E-04 x (N x (V t - V tb ) x (V soln / V a )) / V m(std) = 1.089E-06 lb/dscf F c -factor = 2310 dscf/MMBtu E H2SO4 = C H2SO4 x F c -factor x (100/%CO 2 ) = 0.02796 lb/MMBtu E H2SO4 = C H2SO4 x Q s(std) x 60 = 58 lb/hr

### LABORATORY ANALYSIS

## Laboratory Services 5012 Causeway Blvd * Tampa Fl. 33619 * Ph (813)630-7378 * Fax (813)630-7360 * DOH #E54272 Report For: David Smith, Air Services 

## Laboratory ID: AA99223

Date and Time Collected: Sampled By: 

### Sample Information JORGE VARINO Description: 

### Location Code: 02/17/2009 Report Date:

Polk Sulfuric Acid Plant Reference Method 6 

### TE_PPS_SAP_RM6

Project Account Code: 01/19/2009 Date of Sample Receipt: Sample Collection Method: 

### Laboratory Results 01/15/2009 10:00:00 AM

Result PARAMETER Qualifier Code Test Method Analyst Units Upper Limit MDL Violation Check Analysis Date & Time Lower Limit Normality of BaCl2 * 2H2O 0.0001 KACLH 0.0102 0 1/20/2009 11:00:00 A M SO3, Avg. of Blank Titrations milliliters 0.01 EPA - Meth.8 KACLH 0.02 I 0 1/20/2009 11:00:00 A M SO3, Run #1, Avg. of Titrations milliliters 0.01 EPA - Meth.8 KACLH 2.7 0 1/20/2009 11:00:00 A M SO3, Run #2, Avg. of Titrations milliliters 0.01 EPA - Meth.8 KACLH 1.52 0 1/20/2009 11:00:00 A M SO3, Run #3, Avg. of Titrations milliliters 0.01 EPA - Meth.8 KACLH 0.80 0 1/20/2009 11:00:00 A M SO3, Run #4, Avg. of Titrations milliliters 0.01 EPA - Meth.8 KACLH 2.88 0 1/20/2009 11:00:00 A M SO3, Run #5, Avg. of Titrations milliliters 0.01 EPA - Meth.8 KACLH 4.92 0 1/20/2009 11:00:00 A M SO3, Run #6, Avg. of Titrations milliliters 0.01 EPA - Meth.8 KACLH 5.75 0 1/20/2009 11:00:00 A M SO3, Run #7, Avg. of Titrations milliliters 0.01 EPA - Meth.8 KACLH 7.78 0 1/20/2009 11:00:00 A M SO3, Volume of Contained Sample milliliters 1 EPA - Meth.8 KACLH 500 0 1/20/2009 11:00:00 A M SO3, Volume of Sample Aliquot milliliters 0.1 EPA - Meth.8 KACLH see comments 0 1/20/2009 11:00:00 A M 

### Comments

Ray McDarby,

Manager, Laboratory Services I - The reported value is between the laboratory method detection limit (MDL) and the laboratory pr actical quantitation limit ( PQL). PQL = 4 x MDL. All results calculated on a wet to wet basis, unless otherwise indicated. Data Qualifier Codes Explanation:
Should there be any questions regar ding this report, please contact:

(813) 630-7878 For Peggy Penner,

Report Number: Page 1 of 1 "General Report" AA99223-021709-11 All of the results presented in this r eport pertain to results for sample AA99223

### EQUIPMENT CALIBRATIONS

### Environmental Service s A ir Services Grou p


## SUMMARY OF E Q UIPMENT CALIBRATION S

EQUIPMENT CAL DATE METHOD RESULTS CONSOLE (MB 07) USEPA RM 5 INITIA L 10/24/2008 (ORIFICE) 0.974 POST TEST 01/22/2009 0.978 NOZZLE (SN16) CALIPER INITIA L 10/24/2008 MEASUREMENTS 0.197 POST TEST 01/19/2009 0.198
PYROMETER (PY 09) 10/24/2008 ASTM THERMOMETER + 2 o 

### F
PITOT TUBE (PT 1 0 ) 10/24/2008 USEPA RM 2 C p 

### = 0.84
BAROMETER (BR 06) 01/05/2009 NWS COMPARISON + 0.01" Hg

### Environmental Services Air Services Group

Blue Team Manufacturer: Thermo Anderson Calibration Date: Model Number:MST-C1 Barometric Pressure: 29.93 "Hg Instrument Code Number: ^MB07 Theoretical Critical Vacuum: 14.12 "Hg LabWorks Sample Number: Calibrated By:

Initial Final Total Δ H Time Volume Volume Volume Inlet Outlet Inlet Outlet "H 2 

### O Minutes ft 3 

### ft 3 

### ft 3 

### oF oF oF oF 0.63 15 130.700 137.750 7.050 79 74 80 75 1.15 15 154.500 163.894 9.394 86 77 85 78 1.90 15 141.910 153.917 12.007 83 75 86 77 3.55 15 164.650 181.150 16.500 86 79 94 81

Orifice K' A ctual Serial Orifice Vacuum Initial Final Average Number Coefficient "Hg oF oF oF 48 0.3448 23.0 72 72 72.0 55 0.4593 21.5 72 72 72.0 63 0.5917 19.5 72 72 72.0 73 0.8101 16.5 72 72 72.0
Dry Gas Meter Calibration Calibration Volume Volume Volume Y Δ H α Corrected Corrected Nominal Value QA/QC Value QA/QC Vm (std) , ft 3 Vcr (std) , ft 3 Vcr (std) , ft 3 

### (ratio) + 0.02 "H 2 

### O + 0.2

6.942 6.711 6.763 0.967 -0.007 1.741 -0.019 9.185 8.940 9.008 0.973 0.000 1.776 0.016 11.789 11.517 11.605 0.977 0.003 1.772 0.012 16.124 15.768 15.889 0.978 0.004 1.751 -0.009 Averages: 0.974 1.760

Review/Approval:

For Calibration Y, the ratio of the reading of the calibration orifice to the dry gas meter, acceptable tolerance from average is + 0.02. For Calibration Δ H α , the acceptable tolerance of individual values from the average is + 0.2.



### 29-Oct-08 Critical Orifice Readings Ambient Temperatures

CALCULATED DATA Critical Orifice The Critical Orifice Coefficient, K', should be in English units. 

### IMPORTANT Dry Gas Meter Readings Initial Temperatures Final Tempertures 10/24/2008

GDB

IMPORTANT For valid test results, the Actual Vacuum should be 1 to 2 "Hg greater than the Theoretical Critical Vacuum Shown above. 

### USEPA Reference Method 5

Dry Gas Meter Calibration

Critical Orifice Method Quarterly Calibration

### Environmental Services Air Services Group

Manufacturer: THERMO Calibration Date: Model Number:MST Barometric Pressure: 30.35 "Hg Instrument Code Number: MB07 Theoretical Critical Vacuum: 14.32 "Hg LabWorks Sample Number: Calibrated By: A ssociated Test: Team: BLUE

Initial Final Total Δ H Time Volume Volume Volume Inlet Outlet Inlet Outlet "H 2 

### O Minutes ft 3 

### ft 3 

### ft 3 

### oF oF oF oF

1.9 10 383.300 391.225 7.925 76 72 77 72 1.9 10 391.225 399.151 7.926 78 72 79 74 1.9 10 399.151 407.143 7.992 79 74 80 74

Orifice K' A ctual Serial Orifice Vacuum Initial Final Average Number Coefficient "Hg oF oF oF 63 0.5924 18.0 71 71 71.0 63 0.5924 18.0 71 71 71.0 63 0.5924 18.0 71 71 71.0

Dry Gas Meter Calibration Calibration Volume Volume Volume Y Δ H α Corrected Corrected Nominal Value QA/QC Value QA/QC Vm (std) , ft 3 Vcr (std) , ft 3 Vcr (std) , ft 3 

### (ratio) + 0.02 "H 2 

### O + 0.2

7.978 7.802 7.739 0.978 0.000 1.760 0.004 7.957 7.802 7.739 0.981 0.003 1.755 -0.001 8.008 7.802 7.739 0.974 -0.003 1.752 -0.004 Averages: 0.978 1.756 Prior Y: 0.974 % Difference:(+/-5%) -0.37% PASS

Review/Approval: Date: IMPORTANT

IMPORTANT For valid test results, the Actual Vacuum should be 1 to 2 "Hg greater than the Theoretical Critical Vacuum Shown above. The Critical Orifice Coefficient, K', should be in English units.



### Ambient Temperatures Dry Gas Meter Readings Final Tempertures Initial Temperatures

Critical Orifice Readings 

### USEPA Reference Method 5

Dry Gas Meter Calibration

Critical Orifice Method

SEG 01/22/2009 

### POST - TEST CALIBRATION CHECK

23-Jan-09 CALCULATED DATA

For Calibration Y, the ratio of the reading of the calibration orifice to the dry gas meter, acceptable tolerance from average is + 0.02. For Calibration Δ H α , the acceptable tolerance of individual values from the average is + 0.2. 

### Critical Orifice

### Calibration Date: Responsible Party:

Nozzle Maximum 

### Average

I.D. D 1 

### D 2 

### D 3 D ifference, " 

### D n 

### , inches ^SN01 0.110 0.110 0.119 0.004 0.113 ^SN04 0.121 0.121 0.120 0.000 0.121 ^SN05 0.147 0.147 0.145 0.001 0.146 ^SN06 0.197 0.196 0.195 0.001 0.196 ^SN09 0.270 0.270 0.271 0.000 0.270 ^SN10 0.294 0.295 0.296 0.001 0.295 ^SN12 0.387 0.386 0.388 0.001 0.387 ^SN15 0.163 0.164 0.163 0.000 0.163 ^SN16 0.198 0.197 0.197 0.000 0.197 ^SN19 0.278 0.280 0.279 0.001 0.279 ^SN22 0.366 0.366 0.367 0.000 0.366 ^SN30 0.311 0.310 0.312 0.001 0.311 ^SN36 0.184 0.184 0.182 0.001 0.183 ^SN37 0.210 0.209 0.209 0.000 0.209 ^SN38 0.252 0.250 0.252 0.001 0.251 ^SN46 0.189 0.188 0.187 0.001 0.188 ^SN47 0.203 0.204 0.203 0.000 0.203 ^SN48 0.252 0.252 0.251 0.000 0.252 ^SN50 0.309 0.311 0.312 0.001 0.311 ^SN58 0.243 0.246 0.246 0.001 0.245 ^SN68 0.252 0.250 0.250 0.001 0.251 ^SN69 0.371 0.370 0.374 0.002 0.372 ^SN70 0.616 0.614 0.614 0.001 0.615 ^SN71 0.614 0.614 0.612 0.001 0.613 ^SN72 0.372 0.372 0.373 0.000 0.372 ^SN73 0.510 0.510 0.509 0.000 0.510 ^SN74 0.483 0.482 0.482 0.000 0.482



### QA/QC Review by: 29-Oct-08 Nozzle Diameter, D n 

### (in) QUARTERLY NOZZLE CALIBRATIONS

STEEL NOZZLE SET

10/24/2008 RN/JV

### Environmental Service s A ir Services Grou p

Shared Resource Calibration Date: Calibration Personnel: Test Designation:

Maximum 

### Average D 1 

### D 2 

### D 3 Difference, " 

### D n 

### , inches 0.197 0.198 0.198 0.001 0.198

Data Notations: Maximum Difference must be < 0.004".



### Quarterly (pre-test) value for nozzle ID SN16 was 0.197

Difference (Pre-test/Post-test) is: -0.001 PASS

QA/QC Review by: 23-Jan-09 POST TEST NOZZLE CALIBRATION

Nozzle Identifier Nozzle Diameter, D n 

### (in) 01/19/2009 SEG Polk Unit 1 - 01-(15-16)-09 sam



### SN16

### Environmental Services A ir Services Group

Blue Team Pyrometer Under Tes t Pyrometer Number: ^PY09 Labworks Sample # Calibration Date: 10/24/2008

Calibrator Information Calibrator Type/Manufacturer: Hart Scientific Calibrator Serial Number: A OA024 Date of Last Calibration: 04/28/2008 Calibration Personnel (Typed and Signature):

Calibration Data
Calibration Reference Pyrometer Point Temperature Indication Difference

1 

### 400 402 -2 2 

### 212 214 -2 3 

### 32 33 -1
Reference temperatures must encompass the expected range of measurement. These three points should be ~ 32 degrees, ~212 degrees, and ~ 400 degrees Farenheit. Difference is calculated as follows:
(reference temperature ) – (pyrometer indication )

Qaulity Control Data

Calibration Point Difference

1 

### Pass 2 

### Pass 3 

### Pass

Reviewer: 

### 0

Varino 

### Pyrometer Calibration

29-Oct-08Environmental Services Air Services Group

Pitot Tube ID # Calibration Date Operating Quarter/Year: 4-08 Openings Damaged? ___ Y __

_ N Repaired? ___

_ Y ___ N ___ N/A

Labworks #:
Alpha and Beta Angle Determinations Acceptable Limits:

α 1 0 degrees Dt 0.48 < Dt > 0.95 cm

α 2 0.6 degrees α < 10 degrees β 1 1.4 degrees β 2 1.3 degrees β 1 < 5 degrees (alongside top impact openings) Gamma, Theta, Α
, Ζ , and W Determination s β 2 < 5 degrees (alongside bottom impact openings)

ψ 0.5 degrees Ζ < 0.32 cm ( Α sin ψ ) Α 2.43 cm W < 0.08 cm (Asin ο ) Ζ 0.021 cm Α distance between tips

ο angle of plane on side of pitots

ο 0.1 degrees ψ angle between tips W 0.004 cm

Comments:

Calibrated by:

Q uality Assurance Review / Approval: ( α 1 measured across top impact openings) PITOT TUBE CALIBRATION DATA SHEET

PT10 Shared Resource

10/24/2008

Pass Pass Pass

Pass 0

Pass ( α 2 measured across bottom impact openings)

REMOVABLE Pass

NOTES All measurements are taken in accordance with the requirements of 40 CFR 60, Appendix A - Test Methods, Method 2, "Determination of stack gas velocity and volumetric flow rate (Type S pitot tube)". Measurement details are found in EPA/600/4-77/027b, "Quality Assurance Handbook for Air Pollution Measurement Systems: Stationary Source Specific Methods", sub-section 3.1.1, Procuement of Apparatus and Supplies.

29-Oct-08

### Environmental Services Air Services Group

Blue Team Instrument Number: Calibration Date: Calibration Personnel: Labworks #: Difference T ime "H g 9:00 0.03 10:15 0.02 11:40 0.01

Avera g e Difference: 0.02

Note: Barometric readin g s must a g ree within ± 0.1 "H g

. Current Reference is National Weather Service, TIA. Comments (Note any ad j ustments):

QA/QC Review by: Date: 6-Jan-09 Current Conditions at Tampa International Airport 30.18 30.17 30.20 30.17 30.20 30.18 Barometer Readin g Reference Readin g Inches Mercury Inches Mercury BAROMETER CALIBRATION

^BR06 01/05/2009 SEG

### METHOD 8B DATA

## Polk Power Station Unit #1 Run 1 Data Calculated from Source Measurements: Barometric Pressure, P b : 30.02 Sample Volume, V m : 3.24 Average Orifice Meter, Δ H: 0.055 Average Meter Temp., T m : 55 Meter Box Y: 0.996

Q s(std) From External Source: 47763686

Data from Laboratory Analysis: H 2 SO 4 SO 2 Normality of Barium Chloride titrant, N 0.0102 0.0103 Volume Titrant Blank, V tb 0.02 0.01 Volume Titrant Sample, V t 0.5 1.00 Volume of Sample Aliquot, V a 50 20 Total Volume of Solution, V soln 250 500

Data Calculated: V m(std) = 17.647 x V m x Y x (P b + ( Δ H / 13.6)) / (T m +460) = 3.320 7.971E-07 5.422E-06

38.071 lbs/hr 258.96 lbs/hr 

### 16-Jan-2009

Calculated SO 2 Emission Rate, E= C H2SO4 = 1.081E-04 x (N x (V t - V tb ) x (V soln / V a )) / Vm (std) =

C SO2 = 7.061E-05 x (N x (V t - V tb ) x (V soln / V a )) / Vm (std) =

Calculated H 2 SO 4 Emission Rate, E=

## Polk Power Station Unit #1 Run 2 Data Calculated from Source Measurements: Barometric Pressure, P b : 30.01 Sample Volume, V m : 4.871 Average Orifice Meter, Δ H: 0.075 Average Meter Temp., T m : 60 Meter Box Y: 0.996

Q s(std) From External Source: 47405194

Data from Laboratory Analysis: H 2 SO 4 SO 2 Normality of Barium Chloride titrant, N 0.0102 0.0103 Volume Titrant Blank, V tb 0.02 0.01 Volume Titrant Sample, V t 0.75 1.75 Volume of Sample Aliquot, V a 50 20 Total Volume of Solution, V soln 250 500

Data Calculated: V m(std) = 17.647 x V m x Y x (P b + ( Δ H / 13.6)) / (T m +460) = 4.942 8.144E-07 6.402E-06

38.606 lbs/hr 303.48 lbs/hr Calculated SO 2 Emission Rate, E= 

### 16-Jan-2009

C H2SO4 = 1.081E-04 x (N x (V t - V tb ) x (V soln / V a )) / Vm (std) =

C SO2 = 1.081E-04 x (N x (V t - V tb ) x (V soln / V a )) / Vm (std) =

Calculated H 2 SO 4 Emission Rate, E=

## Polk Power Station Unit #1 Run 3 Data Calculated from Source Measurements: Barometric Pressure, P b : 

### 30.15 Sample Volume, V m : 

### 5.15 Average Orifice Meter, Δ H: 

### 0.085 Average Meter Temp., T m : 

### 67 Meter Box Y: 

### 0.996

Q s(std) From External Source: 

### 47350478

Data from Laboratory Analysis: H 2 SO 4 SO 2 Normality of Barium Chloride titrant, N 0.0102 0.0103 Volume Titrant Blank, V tb 0.02 0.01 Volume Titrant Sample, V t 0.78 1.6 Volume of Sample Aliquot, V a 50 20 Total Volume of Solution, V soln 250 500

Data Calculated: V m(std) = 17.647 x V m x Y x (P b + ( Δ H / 13.6)) / (T m +460) = 5.180 8.089E-07 5.581E-06

38.303 lbs/hr 264.28 lbs/hr Calculated SO 2 Emission Rate, E= 

### 16-Jan-2009

C H2SO4 = 1.081E-04 x (N x (V t - V tb ) x (V soln / V a )) / Vm (std) =

C SO2 = 1.081E-04 x (N x (V t - V tb ) x (V soln / V a )) / Vm (std) =

Calculated H 2 SO 4 Emission Rate, E=

### Flow From CEMS

Date Time FLO1 Date Time FLO1 Date Time FLO1

01/16/2009 9:41 790.3 01/16/2009 11:02 794.7 01/16/2009 12:15 795.9 01/16/2009 9:42 796.4 01/16/2009 11:03 783.4 01/16/2009 12:16 793.6 01/16/2009 9:43 805.2 01/16/2009 11:04 789.8 01/16/2009 12:17 788.4 01/16/2009 9:44 795.8 01/16/2009 11:05 790.8 01/16/2009 12:18 791.1 01/16/2009 9:45 794.2 01/16/2009 11:06 795.3 01/16/2009 12:19 791.7 01/16/2009 9:46 789 01/16/2009 11:07 801.1 01/16/2009 12:20 795.3 01/16/2009 9:47 782.9 01/16/2009 11:08 788.3 01/16/2009 12:21 791.4 01/16/2009 9:48 786.5 01/16/2009 11:09 786.9 01/16/2009 12:22 785.3 01/16/2009 9:49 785.5 01/16/2009 11:10 788.4 01/16/2009 12:23 780.9 01/16/2009 9:50 786.2 01/16/2009 11:11 792 01/16/2009 12:24 778.8 01/16/2009 9:51 791.9 01/16/2009 11:12 804.6 01/16/2009 12:25 778.1 01/16/2009 9:52 794 01/16/2009 11:13 786.3 01/16/2009 12:26 783.1 01/16/2009 9:53 797.5 01/16/2009 11:14 785.3 01/16/2009 12:27 791.3 01/16/2009 9:54 798 01/16/2009 11:15 782.5 01/16/2009 12:28 795.9 01/16/2009 9:55 786.4 01/16/2009 11:16 781.3 01/16/2009 12:29 793.3 01/16/2009 9:56 797.4 01/16/2009 11:17 789.3 01/16/2009 12:30 793.7 01/16/2009 9:57 795.5 01/16/2009 11:18 792.1 01/16/2009 12:31 796.2 01/16/2009 9:58 795.8 01/16/2009 11:19 781.8 01/16/2009 12:32 791.6 01/16/2009 9:59 789.5 01/16/2009 11:20 783.2 01/16/2009 12:33 786.1 01/16/2009 10:00 790.6 01/16/2009 11:21 786.1 01/16/2009 12:34 779.8 01/16/2009 10:01 788.2 01/16/2009 11:22 789.1 01/16/2009 12:35 789.4 01/16/2009 10:02 804.1 01/16/2009 11:23 794.4 01/16/2009 12:36 796.1 01/16/2009 10:03 790.5 01/16/2009 11:24 792.6 01/16/2009 12:37 797.2 01/16/2009 10:04 794.2 01/16/2009 11:25 775.7 01/16/2009 12:38 788.3 01/16/2009 10:05 792.5 01/16/2009 11:26 787.1 01/16/2009 12:39 792.5 01/16/2009 10:06 792.5 01/16/2009 11:27 790.5 01/16/2009 12:40 793.9 01/16/2009 10:07 793.5 01/16/2009 11:28 790.9 01/16/2009 12:41 791.8 01/16/2009 10:08 794.9 01/16/2009 11:29 788.8 01/16/2009 12:42 780 01/16/2009 10:09 794.5 01/16/2009 11:30 792 01/16/2009 12:43 781.5 01/16/2009 10:10 801.4 01/16/2009 11:31 793.6 01/16/2009 12:44 778.9 01/16/2009 10:11 793.9 01/16/2009 11:32 797.3 01/16/2009 12:45 777 793.1871 789.5226 788.6484 47591226 47371355 47318903

## Laboratory Services 5012 Causeway Blvd * Tampa Fl. 33619 * Ph (813)630-7378 * Fax (813)630-7360 * DOH #E54272 Report For: David Smith, Air Services 

## Laboratory ID: AA99221

Date and Time Collected: Sampled By: 

### Sample Information JORGE VARINO Description: 

### Location Code: 02/18/2009 Report Date:

Polk Sulfuric Acid Plant Reference Method 6 

### TE_PPS_SAP_RM6

Project Account Code: 01/19/2009 Date of Sample Receipt: Sample Collection Method: 

### Laboratory Results 01/14/2009 10:00:00 AM

Result PARAMETER Qualifier Code Test Method Analyst Units Upper Limit MDL Violation Check Analysis Date & Time Lower Limit Normality of BaCl2 * 2H2O 0.0001 KACLH 0.0102 0 1/20/2009 11:00:00 A M SO3, Avg. of Blank Titrations milliliters 0.01 EPA - Meth.8 KACLH 0.02 I 0 1/20/2009 11:00:00 A M SO3, Run #1, Avg. of Titrations milliliters 0.01 EPA - Meth.8 KACLH 0.19 0 1/20/2009 11:00:00 A M SO3, Run #2, Avg. of Titrations milliliters 0.01 EPA - Meth.8 KACLH 0.18 0 1/20/2009 11:00:00 A M SO3, Run #3, Avg. of Titrations milliliters 0.01 EPA - Meth.8 KACLH 0.30 0 1/20/2009 11:00:00 A M SO3, Run #4, Avg. of Titrations milliliters 0.01 EPA - Meth.8 KACLH 0.35 0 1/20/2009 11:00:00 A M SO3, Run #5, Avg. of Titrations milliliters 0.01 EPA - Meth.8 KACLH 0.28 0 1/20/2009 11:00:00 A M SO3, Run #6, Avg. of Titrations milliliters 0.01 EPA - Meth.8 KACLH 0.20 0 1/20/2009 11:00:00 A M SO3, Run #7, Avg. of Titrations milliliters 0.01 EPA - Meth.8 KACLH 0.40 0 1/20/2009 11:00:00 A M SO3, Run #8, Avg. of Titrations milliliters 0.01 EPA - Meth.8 KACLH 0.50 0 1/20/2009 11:00:00 A M SO3, Volume of Contained Sample milliliters 1 EPA - Meth.8 KACLH 250 0 1/20/2009 11:00:00 A M SO3, Volume of Sample Aliquot milliliters 0.1 EPA - Meth.8 KACLH 50 0 1/20/2009 11:00:00 A M 

### Comments

Ray McDarby,

Manager, Laboratory Services I - The reported value is between the laboratory method detection limit (MDL) and the laboratory pr actical quantitation limit ( PQL). PQL = 4 x MDL. All results calculated on a wet to wet basis, unless otherwise indicated. Data Qualifier Codes Explanation:
Should there be any questions regar ding this report, please contact:

(813) 630-7878 For Peggy Penner,

Report Number: Page 1 of 1 "General Report" AA99221-021809-13 All of the results presented in this r eport pertain to results for sample AA99221

## Laboratory Services 5012 Causeway Blvd * Tampa Fl. 33619 * Ph (813)630-7378 * Fax (813)630-7360 * DOH #E54272 Report For: David Smith, Air Services 

## Laboratory ID: AA99222

Date and Time Collected: Sampled By: 

### Sample Information JORGE VARINO Description: 

### Location Code: 02/18/2009 Report Date:

Polk Sulfuric Acid Plant Reference Method 6 

### TE_PPS_SAP_RM6

Project Account Code: 01/19/2009 Date of Sample Receipt: Sample Collection Method: 

### Laboratory Results 01/16/2009 10:00:00 AM

Result PARAMETER Qualifier Code Test Method Analyst Units Upper Limit MDL Violation Check Analysis Date & Time Lower Limit Normality of BaCl2 * 2H2O 0.0001 KARXL 0.0103 0 1/20/2009 11:45:00 A M SO2, Avg. of Blank Titrations milliliters 0.1 EPA Method 6 KARXL 0.01 0 1/20/2009 11:45:00 A M SO2, Final Sample Volume milliliters 0.1 EPA Method 6 KARXL see comment 0 1/20/2009 11:45:00 A M SO2, Run 1, Avg. of Titrations milliliters 0.01 EPA Method 6 KARXL 1.0 0 1/20/2009 11:45:00 A M SO2, Run 2, Avg. of Titrations milliliters 0.01 EPA Method 6 KARXL 1.75 0 1/20/2009 11:45:00 A M SO2, Run 3, Avg. of Titrations milliliters 0.01 EPA Method 6 KARXL 1.6 0 1/20/2009 11:45:00 A M SO2, Run 4, Avg. of Titrations milliliters 0.01 EPA Method 6 KARXL 3.95 0 1/20/2009 11:45:00 A M SO2, Volume of Sample Aliquot milliliters 0.1 EPA Method 6 KARXL see comment 0 1/20/2009 11:45:00 A M 

### Comments

Ray McDarby,

Manager, Laboratory Services All results calculated on a wet to wet basis, unless otherwise indicated. Should there be any questions regar ding this report, please contact:

(813) 630-7878 For Peggy Penner,

Report Number: Page 1 of 1 "General Report" AA99222-021809-13 All of the results presented in this r eport pertain to results for sample AA99222

## APPENDIX C

TURBINE DATA

### PI Ops Data Run 1

Plant Information Source: polk-1pisrv Start Time: 01/15/2009 12:45

End Time: 01/15/2009 13:51 Time Interval: 1m

Tag Name: 1pwrji900 1TSYFI100 1tmsti922m 1tsyai202 Tag Explanation: Unit Load Fuel Flow Inlet Temp Satuator Tag Units: Mwe KCFH oF % H2O Run Average: 168.142712 6525.49482 65.8596765 2.64351407 15-Jan-09 12:45:00 167.3644104 6468.72021 64.893837 2.43872595 15-Jan-09 12:46:00 166.8514099 6473.58154 65.0991592 2.43878102 15-Jan-09 12:47:00 167.4471283 6483.01025 64.9707336 2.43883586 15-Jan-09 12:48:00 168.2921753 6520.29395 65.0935211 2.43889093 15-Jan-09 12:49:00 168.6584015 6500.03467 65.2163162 2.43894577 15-Jan-09 12:50:00 169.0246277 6511.40186 65.3391037 2.43900084 15-Jan-09 12:51:00 168.6378937 6523.06348 65.4618988 2.43905592 15-Jan-09 12:52:00 168.2107391 6518.41797 65.2326202 2.43911076 15-Jan-09 12:53:00 168.0377045 6490.62354 65.0786285 2.43916583 15-Jan-09 12:54:00 168.0682983 6495.58545 64.9854279 2.43922067 15-Jan-09 12:55:00 168.0403748 6497.27246 65.4394073 2.43927574 15-Jan-09 12:56:00 167.9596252 6492.50537 65.8249207 2.43933058 15-Jan-09 12:57:00 167.9084167 6530.22461 65.2531509 2.45538712 15-Jan-09 12:58:00 168.0899658 6546.22461 65.5662689 2.47677755 15-Jan-09 12:59:00 168.4925995 6558.4873 66.1736908 2.49816799 15-Jan-09 13:00:00 168.4293671 6543.07715 65.5865173 2.51955843 15-Jan-09 13:01:00 168.8476105 6544.15869 65.8557205 2.54094887 15-Jan-09 13:02:00 167.9534302 6529.47412 65.5862274 2.56233907 15-Jan-09 13:03:00 167.8424835 6501.18701 66.124054 2.58372951 15-Jan-09 13:04:00 168.8517914 6518.88232 66.0452194 2.60511994 15-Jan-09 13:05:00 168.226532 6508.66992 65.8912201 2.62651038 15-Jan-09 13:06:00 167.4694366 6478.05273 65.4740143 2.64790058 15-Jan-09 13:07:00 166.860672 6474.77051 65.0163193 2.66929102 15-Jan-09 13:08:00 168.3968506 6505.53516 65.4533386 2.69068146 15-Jan-09 13:09:00 168.5484467 6534.0625 65.5662689 2.7120719 15-Jan-09 13:10:00 169.8215179 6525.70215 65.0118942 2.71718478 15-Jan-09 13:11:00 168.9063721 6517.33447 65.2938385 2.71734381 15-Jan-09 13:12:00 168.8286591 6534.82666 65.7553177 2.71750283 15-Jan-09 13:13:00 168.7964325 6528.01465 65.7823105 2.71766162 15-Jan-09 13:14:00 167.5170135 6521.30225 65.4523544 2.71782064 15-Jan-09 13:15:00 167.5018616 6505.38818 65.2531509 2.71797967 15-Jan-09 13:16:00 167.0470734 6507.80859 65.3627396 2.71813846 15-Jan-09 13:17:00 166.5923004 6521.00879 65.7590714 2.71829748 15-Jan-09 13:18:00 167.6369324 6504.17822 66.0888519 2.71845651



### Page 1 of 2

### PI Ops Data Run 1

Tag Name: 1pwrji900 1TSYFI100 1tmsti922m 1tsyai202 Tag Explanation: Unit Load Fuel Flow Inlet Temp Satuator Tag Units: Mwe KCFH oF % H2O 15-Jan-09 13:19:00 167.0618896 6493.47119 65.9348526 2.71861529 15-Jan-09 13:20:00 168.084198 6513.10693 66.183815 2.71877432 15-Jan-09 13:21:00 168.8658905 6542.2583 66.496933 2.71893334 15-Jan-09 13:22:00 168.8939056 6527.38916 66.1684113 2.71909213 15-Jan-09 13:23:00 168.8278656 6542.42285 65.8706894 2.71925116 15-Jan-09 13:24:00 168.7618256 6544.47656 65.8706894 2.71941018 15-Jan-09 13:25:00 168.9595337 6548.05811 65.8706894 2.71956897 15-Jan-09 13:26:00 168.1079865 6539.39404 65.8396072 2.71972799 15-Jan-09 13:27:00 167.4126434 6505.13184 66.1170807 2.71988702 15-Jan-09 13:28:00 167.7828217 6521.44922 65.963089 2.72004604 15-Jan-09 13:29:00 167.8647156 6516.82861 65.9938889 2.72020483 15-Jan-09 13:30:00 167.5659027 6503.4082 66.7227859 2.72036386 15-Jan-09 13:31:00 167.2670898 6503.79785 66.6847992 2.72052288 15-Jan-09 13:32:00 168.1742401 6530.72607 66.0811539 2.72068167 15-Jan-09 13:33:00 168.9823456 6548.20752 65.9682236 2.72084069 15-Jan-09 13:34:00 169.3472443 6556.45752 65.9161453 2.72099972 15-Jan-09 13:35:00 167.8694305 6529.50391 66.0676575 2.7211585 15-Jan-09 13:36:00 167.7674561 6524.57178 66.3299332 2.72131753 15-Jan-09 13:37:00 167.9418182 6513.60205 66.463295 2.72147655 15-Jan-09 13:38:00 167.4452667 6536.70313 66.3080292 2.72163534 15-Jan-09 13:39:00 167.5704498 6526.42383 66.3840027 2.72179437 15-Jan-09 13:40:00 168.3495789 6544.5957 65.9733505 2.72195339 15-Jan-09 13:41:00 169.0258789 6556.4668 66.4738312 2.72211218 15-Jan-09 13:42:00 168.8196564 6541.50586 66.3198395 2.7222712 15-Jan-09 13:43:00 168.6774139 6549.09619 66.4907761 2.72243023 15-Jan-09 13:44:00 168.4714508 6548.021 66.4291763 2.72258925 15-Jan-09 13:45:00 167.7942352 6537.99854 66.3675766 2.72274804 15-Jan-09 13:46:00 168.0614014 6527.97607 66.3059845 2.72290707 15-Jan-09 13:47:00 167.9803467 6566.55078 66.2443848 2.72306609 15-Jan-09 13:48:00 167.5486145 6604.64844 66.1915131 2.72322488 15-Jan-09 13:49:00 168.2042694 6591.52148 66.6534882 2.7233839 15-Jan-09 13:50:00 168.5769196 6580.75928 67.1154709 2.72354293 15-Jan-09 13:51:00 168.3388672 6578.74268 66.810051 2.72370172



### Page 2 of 2

### PI Ops Data Run 2

Plant Information Source: polk-1pisrv Start Time: 01/15/2009 14:37

End Time: 01/15/2009 15:43 Time Interval: 1m

Tag Name: 1pwrji900 1TSYFI100 1tmsti922m 1tsyai202 Tag Explanation: Unit Load Fuel Flow Inlet Temp Satuator Tag Units: Mwe KCFH oF % H2O Run Average: 168.0681159 6550.08427 68.1626202 2.7362589 15-Jan-09 14:37:00 168.6414948 6576.45703 67.5383987 2.73101354 15-Jan-09 14:38:00 168.1415405 6561.39258 67.3341827 2.73117256 15-Jan-09 14:39:00 167.3430634 6512.34912 67.1299744 2.73133135 15-Jan-09 14:40:00 167.3430634 6531.66064 68.0163345 2.73149037 15-Jan-09 14:41:00 167.3359375 6496.27637 67.7650681 2.7316494 15-Jan-09 14:42:00 167.3134155 6497.10156 67.4362946 2.73180819 15-Jan-09 14:43:00 167.5065155 6518.24658 67.5466537 2.73196721 15-Jan-09 14:44:00 168.2449646 6529.4126 68.0086365 2.73212624 15-Jan-09 14:45:00 169.098999 6563.40918 67.8418121 2.73228502 15-Jan-09 14:46:00 169.0547028 6543.39502 67.6174393 2.73244405 15-Jan-09 14:47:00 168.831955 6551.06445 67.4621735 2.73260307 15-Jan-09 14:48:00 168.0484924 6535.96924 67.9493179 2.7327621 15-Jan-09 14:49:00 168.2115021 6538.13916 68.1941071 2.73292089 15-Jan-09 14:50:00 167.3100891 6519.20898 68.4388885 2.73307991 15-Jan-09 14:51:00 168.3791351 6538.09277 68.68367 2.73323894 15-Jan-09 14:52:00 168.5772705 6555.89209 68.9284592 2.73339772 15-Jan-09 14:53:00 168.5949402 6554.94531 68.5707169 2.73355675 15-Jan-09 14:54:00 166.5953064 6488.88184 68.3456573 2.73371577 15-Jan-09 14:55:00 167.8959961 6526.64941 68.3017654 2.73387456 15-Jan-09 14:56:00 168.0270233 6521.11865 68.2578659 2.73403358 15-Jan-09 14:57:00 169.5129242 6568.29834 68.213974 2.73419261 15-Jan-09 14:58:00 168.8218384 6576.32861 68.1700745 2.7343514 15-Jan-09 14:59:00 168.7439575 6567.82178 68.1261826 2.73451042 15-Jan-09 15:00:00 168.6872253 6559.31494 68.082283 2.73466945 15-Jan-09 15:01:00 168.6305084 6550.80811 68.3756561 2.73482823 15-Jan-09 15:02:00 167.1578522 6542.30078 68.3756561 2.73498726 15-Jan-09 15:03:00 167.574234 6537.06982 68.3756561 2.73514628 15-Jan-09 15:04:00 168.8226013 6567.87061 68.3756561 2.73530531 15-Jan-09 15:05:00 168.5605927 6594.51611 68.1099243 2.7354641 15-Jan-09 15:06:00 168.9947357 6579.25293 68.2114792 2.73562312 15-Jan-09 15:07:00 169.5485687 6605.8374 68.3130341 2.73578215 15-Jan-09 15:08:00 168.5757599 6626.44775 68.1315308 2.73594093 15-Jan-09 15:09:00 168.4451752 6582.2627 68.0625305 2.73609996 15-Jan-09 15:10:00 167.4191589 6548.16162 68.3756561 2.73625898



### Page 1 of 2

### PI Ops Data Run 2

Tag Name: 1pwrji900 1TSYFI100 1tmsti922m 1tsyai202 Tag Explanation: Unit Load Fuel Flow Inlet Temp Satuator Tag Units: Mwe KCFH oF % H2O 15-Jan-09 15:11:00 167.0908966 6516.68799 68.3756561 2.73641777 15-Jan-09 15:12:00 168.0058594 6516.96338 68.1549301 2.7365768 15-Jan-09 15:13:00 168.1958771 6546.11426 68.2883911 2.73673582 15-Jan-09 15:14:00 168.0264282 6547.00049 68.1035995 2.73689461 15-Jan-09 15:15:00 167.9541779 6527.22998 68.2575912 2.73705363 15-Jan-09 15:16:00 168.1529236 6531.23291 68.3037949 2.73721266 15-Jan-09 15:17:00 168.3516541 6568.54297 68.3756561 2.73737144 15-Jan-09 15:18:00 168.5503998 6576.60986 68.3756561 2.73753047 15-Jan-09 15:19:00 168.2329712 6581.22363 68.3756561 2.7376895 15-Jan-09 15:20:00 167.6055756 6551.58398 68.3756561 2.73784852 15-Jan-09 15:21:00 166.9676819 6560.93457 68.1433334 2.73800731 15-Jan-09 15:22:00 167.1508026 6545.16699 68.6577225 2.73816633 15-Jan-09 15:23:00 167.0772552 6505.38232 68.3471832 2.73832536 15-Jan-09 15:24:00 167.0958557 6550.42285 68.3756561 2.73848414 15-Jan-09 15:25:00 167.6451874 6532.9751 68.3756561 2.73864317 15-Jan-09 15:26:00 167.5943756 6543.27246 68.3756561 2.73880219 15-Jan-09 15:27:00 167.7751923 6531.2334 68.0625305 2.73896098 15-Jan-09 15:28:00 168.0791016 6538.1084 68.3705215 2.73912001 15-Jan-09 15:29:00 168.9406281 6566.98438 68.0776825 2.73927903 15-Jan-09 15:30:00 169.0259094 6580.21533 68.1359787 2.73943782 15-Jan-09 15:31:00 169.2017822 6563.89844 68.213295 2.73959684 15-Jan-09 15:32:00 168.1194458 6535.14453 68.2906113 2.73975587 15-Jan-09 15:33:00 168.3254089 6565.54834 68.3679276 2.73991466 15-Jan-09 15:34:00 167.5026093 6554.12012 68.6887741 2.74007368 15-Jan-09 15:35:00 166.4794312 6533.95264 67.9305573 2.74023271 15-Jan-09 15:36:00 167.1668091 6553.29492 67.7752914 2.74039173 15-Jan-09 15:37:00 167.6534424 6538.16943 68.3099976 2.74055052 15-Jan-09 15:38:00 168.3071899 6607.10498 68.2139359 2.74070954 15-Jan-09 15:39:00 168.3854065 6574.8374 68.0074768 2.74086857 15-Jan-09 15:40:00 168.1003418 6560.38965 67.8010254 2.74102736 15-Jan-09 15:41:00 167.8152924 6564.56836 68.1378174 2.74118638 15-Jan-09 15:42:00 167.5886078 6568.74756 68.2404785 2.74134541 15-Jan-09 15:43:00 168.4087067 6552.03027 68.3431473 2.74150419



### Page 2 of 2

### PI Ops Data Run 3

Plant Information Source: polk-1pisrv Start Time: 01/15/2009 15:53

End Time: 01/15/2009 16:59 Time Interval: 1m

Tag Name: 1pwrji900 1TSYFI100 1tmsti922m 1tsyai202 Tag Explanation: Unit Load Fuel Flow Inlet Temp Satuator Tag Units: Mwe KCFH oF % H2O Run Average: 168.0222751 6570.54789 67.6146758 2.74833915 15-Jan-09 15:53:00 167.3086395 6514.61621 67.5911331 2.74309373 15-Jan-09 15:54:00 167.9179993 6532.35693 67.6943588 2.74325275 15-Jan-09 15:55:00 167.0673676 6525.33545 67.9250641 2.74341178 15-Jan-09 15:56:00 167.4351654 6565.42627 67.6195831 2.74357057 15-Jan-09 15:57:00 168.2306519 6597.57178 67.2458649 2.74372959 15-Jan-09 15:58:00 169.026123 6609.12207 67.5525894 2.74388862 15-Jan-09 15:59:00 168.5712585 6590.59863 67.8593216 2.7440474 15-Jan-09 16:00:00 168.3266754 6579.21924 68.1660538 2.74420643 15-Jan-09 16:01:00 167.9620514 6567.5957 68.278923 2.74436545 15-Jan-09 16:02:00 167.0152435 6542.3252 67.9734344 2.74452424 15-Jan-09 16:03:00 167.1053162 6531.28223 67.8041687 2.74468327 15-Jan-09 16:04:00 167.9761505 6547.7583 68.009491 2.74484229 15-Jan-09 16:05:00 168.1389923 6561.19189 68.2148209 2.74500108 15-Jan-09 16:06:00 167.7817078 6545.2583 68.2755585 2.7451601 15-Jan-09 16:07:00 167.9537354 6543.08545 67.8135757 2.74531913 15-Jan-09 16:08:00 168.3369598 6547.96191 67.698082 2.74547815 15-Jan-09 16:09:00 168.7236023 6576.82031 67.5286865 2.74563694 15-Jan-09 16:10:00 168.8079529 6581.35498 68.0488434 2.74579597 15-Jan-09 16:11:00 168.9820557 6588.51465 67.9461823 2.74595499 15-Jan-09 16:12:00 169.0253143 6594.44238 67.8435211 2.74611378 15-Jan-09 16:13:00 168.9460297 6592.97559 67.7558517 2.7462728 15-Jan-09 16:14:00 168.7197418 6576.41406 67.833168 2.74643183 15-Jan-09 16:15:00 167.8488464 6533.92822 67.9104843 2.74659061 15-Jan-09 16:16:00 167.6531372 6541.40869 67.987793 2.74674964 15-Jan-09 16:17:00 167.9672852 6546.65186 68.0520935 2.74690866 15-Jan-09 16:18:00 167.8159943 6612.02539 68.0608215 2.74706745 15-Jan-09 16:19:00 168.362381 6599.58545 67.9581604 2.74722648 15-Jan-09 16:20:00 168.4962158 6562.22363 67.8554993 2.7473855 15-Jan-09 16:21:00 168.6712036 6573.51758 67.7528381 2.74754429 15-Jan-09 16:22:00 168.120697 6569.21387 67.848114 2.74770331 15-Jan-09 16:23:00 167.6468506 6562.55859 67.9502182 2.74786234 15-Jan-09 16:24:00 168.2324982 6603.68311 68.0523224 2.74802136 15-Jan-09 16:25:00 167.9281158 6633.01758 67.7807236 2.74818015 15-Jan-09 16:26:00 168.4043427 6609.4585 67.5271988 2.74833918



### PI Ops Data Run 3

### PI Ops Data Run 3

Tag Name: 1pwrji900 1TSYFI100 1tmsti922m 1tsyai202 Tag Explanation: Unit Load Fuel Flow Inlet Temp Satuator Tag Units: Mwe KCFH oF % H2O 15-Jan-09 16:27:00 167.9824524 6593.32422 67.566124 2.7484982 15-Jan-09 16:28:00 168.3300934 6621.65039 67.7188644 2.74865699 15-Jan-09 16:29:00 167.651123 6607.5332 67.6251984 2.74881601 15-Jan-09 16:30:00 167.466507 6575.91943 67.4699326 2.74897504 15-Jan-09 16:31:00 167.1117249 6527.6665 67.6707077 2.74913383 15-Jan-09 16:32:00 168.4977112 6578.29004 67.5680466 2.74929285 15-Jan-09 16:33:00 168.6829681 6576.65869 67.4653854 2.74945188 15-Jan-09 16:34:00 168.9029236 6589.1377 67.5286865 2.74961066 15-Jan-09 16:35:00 168.4563141 6580.04443 67.6450424 2.74976969 15-Jan-09 16:36:00 168.0097046 6568.31055 67.4923019 2.74992871 15-Jan-09 16:37:00 166.8333588 6538.0957 67.6313553 2.7500875 15-Jan-09 16:38:00 167.464035 6564.57031 67.5563202 2.75024652 15-Jan-09 16:39:00 167.1051636 6544.10986 67.3079681 2.75040555 15-Jan-09 16:40:00 168.3166046 6570.33154 67.6599503 2.75056458 15-Jan-09 16:41:00 168.6320343 6574.01221 67.5065842 2.75072336 15-Jan-09 16:42:00 168.3193054 6560.65918 67.3532181 2.75088239 15-Jan-09 16:43:00 168.3092804 6575.5708 67.199852 2.75104141 15-Jan-09 16:44:00 168.2543793 6580.39893 67.2771683 2.7512002 15-Jan-09 16:45:00 167.5733795 6567.25928 67.2874298 2.75135922 15-Jan-09 16:46:00 167.0635986 6538.81104 67.4165421 2.75151825 15-Jan-09 16:47:00 167.9186554 6542.05029 67.3726425 2.75167704 15-Jan-09 16:48:00 168.0651703 6583.56592 67.3287506 2.75183606 15-Jan-09 16:49:00 168.4687347 6587.70801 67.2848511 2.75199509 15-Jan-09 16:50:00 168.6050262 6574.63574 67.2409592 2.75215387 15-Jan-09 16:51:00 168.0552368 6560.15186 67.1970596 2.7523129 15-Jan-09 16:52:00 167.6744843 6560.36768 67.1531677 2.75247192 15-Jan-09 16:53:00 168.4433441 6562.21631 67.3248444 2.75263071 15-Jan-09 16:54:00 167.8105927 6571.4458 67.0240173 2.75278974 15-Jan-09 16:55:00 167.4368591 6581.3457 67.0344543 2.75294876 15-Jan-09 16:56:00 166.9379578 6569.73438 66.8536835 2.75310779 15-Jan-09 16:57:00 167.3247528 6541.37793 67.0076752 2.75326657 15-Jan-09 16:58:00 167.5229797 6617.49463 67.0461731 2.7534256 15-Jan-09 16:59:00 167.7596741 6583.76025 66.9537811 2.75358462



### PI Ops Data Run 3

### PI Ops Data Run 4

Plant Information Source: polk-1pisrv Start Time: 01/16/2009 9:38

End Time: 01/16/2009 10:47 Time Interval: 1m

Tag Name: 1pwrji900 1TSYFI100 1tmsti922m 1tsyai202 Tag Explanation: Unit Load Fuel Flow Inlet Temp Satuator Tag Units: Mwe KCFH oF % H2O Run Average: 167.9093898 6579.85645 59.1433111 2.82692957 16-Jan-09 09:38:00 168.7384644 6576.45068 57.654068 2.82692957 16-Jan-09 09:39:00 168.5088196 6623.34912 57.4593048 2.82692957 16-Jan-09 09:40:00 167.8095398 6592.01611 57.7647896 2.82692957 16-Jan-09 09:41:00 167.5934143 6585.23291 58.0499878 2.82692957 16-Jan-09 09:42:00 167.3772736 6561.88135 57.7469711 2.82692957 16-Jan-09 09:43:00 167.0917206 6555.00586 57.9789124 2.82692957 16-Jan-09 09:44:00 168.0713043 6590.30518 58.2108498 2.82692957 16-Jan-09 09:45:00 169.20224 6599.50244 58.442791 2.82692957 16-Jan-09 09:46:00 169.1219482 6588.09277 58.6747322 2.82692957 16-Jan-09 09:47:00 168.208786 6562.7124 58.6606636 2.82692957 16-Jan-09 09:48:00 166.9486237 6588.44727 58.4016762 2.82692957 16-Jan-09 09:49:00 167.3802795 6593.57471 58.0911407 2.82692957 16-Jan-09 09:50:00 167.1422272 6562.02783 58.1062889 2.82692957 16-Jan-09 09:51:00 167.5303497 6565.51758 58.3218765 2.82692957 16-Jan-09 09:52:00 167.9184723 6563.97754 58.6298637 2.82692957 16-Jan-09 09:53:00 168.3524323 6587.9585 58.8742027 2.82692957 16-Jan-09 09:54:00 169.1083374 6600.87451 58.6863289 2.82692957 16-Jan-09 09:55:00 168.8677216 6609.8584 59.158577 2.82692957 16-Jan-09 09:56:00 168.581604 6599.52734 59.1973915 2.82692957 16-Jan-09 09:57:00 167.6585541 6584.85986 59.0438194 2.82692957 16-Jan-09 09:58:00 166.7906799 6556.11865 58.8902435 2.82692957 16-Jan-09 09:59:00 167.9839478 6563.4458 58.7366714 2.82692957 16-Jan-09 10:00:00 168.1100159 6603.53613 58.5830956 2.82692957 16-Jan-09 10:01:00 169.2013245 6601.3916 58.4295197 2.82692957 16-Jan-09 10:02:00 167.9585876 6567.89502 58.7698288 2.82692957 16-Jan-09 10:03:00 167.8153992 6583.6626 58.9263878 2.82692957 16-Jan-09 10:04:00 168.1445465 6569.60596 59.3690338 2.82692957 16-Jan-09 10:05:00 168.4687347 6591.95557 59.0777283 2.82692957 16-Jan-09 10:06:00 168.3558807 6593.71094 59.1711617 2.82692957 16-Jan-09 10:07:00 168.3943024 6588.53418 59.1455727 2.82692957 16-Jan-09 10:08:00 168.2934418 6575.14307 59.259819 2.82692957 16-Jan-09 10:09:00 168.1620789 6593.41602 59.1577148 2.82692957 16-Jan-09 10:10:00 168.0307159 6587.41992 59.0556068 2.82692957 16-Jan-09 10:11:00 167.1557465 6575.2373 59.0456505 2.82692957



### Page 1 of 2

### PI Ops Data Run 4

Tag Name: 1pwrji900 1TSYFI100 1tmsti922m 1tsyai202 Tag Explanation: Unit Load Fuel Flow Inlet Temp Satuator Tag Units: Mwe KCFH oF % H2O 16-Jan-09 10:12:00 167.0209656 6569.38037 59.1483116 2.82692957 16-Jan-09 10:13:00 167.2191467 6564.94336 59.2509766 2.82692957 16-Jan-09 10:14:00 166.4516754 6546.17529 59.1913643 2.82692957 16-Jan-09 10:15:00 167.7016296 6579.23779 59.2216644 2.82692957 16-Jan-09 10:16:00 167.9290161 6561.82031 59.4203644 2.82692957 16-Jan-09 10:17:00 167.3394775 6543.42529 58.9994507 2.82692957 16-Jan-09 10:18:00 168.2355042 6627.43799 59.1873245 2.82692957 16-Jan-09 10:19:00 168.2195892 6635.02246 59.3125725 2.82692957 16-Jan-09 10:20:00 168.0143433 6586.88916 59.3125725 2.82692957 16-Jan-09 10:21:00 168.1449127 6570.68408 59.3125725 2.82692957 16-Jan-09 10:22:00 167.6773834 6568.2373 59.5923271 2.82692957 16-Jan-09 10:23:00 167.2707214 6554.87158 59.4383316 2.82692957 16-Jan-09 10:24:00 167.7029724 6566.23877 59.3690376 2.82692957 16-Jan-09 10:25:00 168.093811 6578.43115 59.5751877 2.82692957 16-Jan-09 10:26:00 168.093811 6604.66309 59.3543205 2.82692957 16-Jan-09 10:27:00 168.093811 6598.48828 59.9028816 2.82692957 16-Jan-09 10:28:00 167.5384674 6573.7373 59.6564903 2.82692957 16-Jan-09 10:29:00 167.0809937 6550.27588 59.913147 2.82692957 16-Jan-09 10:30:00 167.7155762 6547.76514 59.6392326 2.82692957 16-Jan-09 10:31:00 168.3315582 6596.646 59.8423347 2.82692957 16-Jan-09 10:32:00 168.9351501 6595.68311 60.0454407 2.82692957 16-Jan-09 10:33:00 168.4353485 6621.94434 60.2485466 2.82692957 16-Jan-09 10:34:00 168.2664185 6556.74805 60.10112 2.82692957 16-Jan-09 10:35:00 167.6598969 6571.41504 59.9477577 2.82692957 16-Jan-09 10:36:00 167.6148682 6581.91455 59.7943916 2.82692957 16-Jan-09 10:37:00 167.5874176 6574.30566 59.6410255 2.82692957 16-Jan-09 10:38:00 168.3930969 6580.30713 59.7185936 2.82692957 16-Jan-09 10:39:00 167.9266052 6576.23682 59.8218231 2.82692957 16-Jan-09 10:40:00 167.18396 6562.12598 59.9250488 2.82692957 16-Jan-09 10:41:00 167.1794739 6541.81836 60.2519302 2.82692957 16-Jan-09 10:42:00 167.0835419 6536.4082 59.8130493 2.82692957 16-Jan-09 10:43:00 167.1634369 6553.0752 59.6590576 2.82692957 16-Jan-09 10:44:00 167.5073395 6570.68799 59.7064972 2.82692957 16-Jan-09 10:45:00 167.8877411 6594.23242 60.077404 2.82692957 16-Jan-09 10:46:00 168.7079163 6600.22168 59.810482 2.82692957 16-Jan-09 10:47:00 168.1721954 6606.21094 60.0568733 2.82692957



### Page 2 of 2

### PI Ops Data Run 5

Plant Information Source: polk-1pisrv Start Time: 01/16/2009 11:05

End Time: 01/16/2009 12:11 Time Interval: 1m

Tag Name: 1pwrji900 1TSYFI100 1tmsti922m 1tsyai202 Tag Explanation: Unit Load Fuel Flow Inlet Temp Satuator Tag Units: Mwe KCFH oF % H2O Run Average: 167.8981858 6563.30103 63.0245156 2.82692957 16-Jan-09 11:05:00 168.7459564 6593.53809 61.2865448 2.82692957 16-Jan-09 11:06:00 168.5748596 6590.12402 61.4045982 2.82692957 16-Jan-09 11:07:00 168.1754608 6606.57861 61.1008911 2.82692957 16-Jan-09 11:08:00 168.2453613 6628.18945 60.9595375 2.82692957 16-Jan-09 11:09:00 167.9863281 6619.38916 61.2646751 2.82692957 16-Jan-09 11:10:00 167.9356537 6592.86621 61.569809 2.82692957 16-Jan-09 11:11:00 168.0443115 6584.18799 61.679348 2.82692957 16-Jan-09 11:12:00 168.1529694 6575.50977 61.2284126 2.82692957 16-Jan-09 11:13:00 168.1258545 6581.08887 61.4308815 2.82692957 16-Jan-09 11:14:00 168.4780426 6590.9834 61.6333542 2.82692957 16-Jan-09 11:15:00 167.849411 6573.23633 61.7952919 2.82692957 16-Jan-09 11:16:00 167.1516876 6552.45459 61.693737 2.82692957 16-Jan-09 11:17:00 167.1210632 6547.87109 61.592186 2.82692957 16-Jan-09 11:18:00 166.9679871 6538.83447 61.5034752 2.82692957 16-Jan-09 11:19:00 167.2507629 6545.13672 61.658741 2.82692957 16-Jan-09 11:20:00 167.8283081 6559.62012 62.1245193 2.82692957 16-Jan-09 11:21:00 168.2344055 6569.8877 62.278511 2.82692957 16-Jan-09 11:22:00 168.5404816 6574.59814 62.4325027 2.82692957 16-Jan-09 11:23:00 167.5231628 6566.05273 62.137104 2.82692957 16-Jan-09 11:24:00 167.4963379 6564.21777 62.9997139 2.82692957 16-Jan-09 11:25:00 167.9642792 6569.55664 62.4864006 2.82692957 16-Jan-09 11:26:00 167.5817719 6574.896 62.293911 2.82692957 16-Jan-09 11:27:00 168.0239258 6580.23486 62.1399193 2.82692957 16-Jan-09 11:28:00 168.2875824 6605.08887 62.6572876 2.82692957 16-Jan-09 11:29:00 168.2387848 6594.63867 62.922718 2.82692957 16-Jan-09 11:30:00 169.5367737 6572.27051 63.1280403 2.82692957 16-Jan-09 11:31:00 168.8678284 6583.61963 63.3333664 2.82692957 16-Jan-09 11:32:00 168.1476898 6562.22998 63.0078506 2.82692957 16-Jan-09 11:33:00 167.153595 6552.04736 62.5496254 2.82692957 16-Jan-09 11:34:00 167.0767975 6551.91992 63.1280403 2.82692957 16-Jan-09 11:35:00 167.5510864 6538.70898 63.1361885 2.82692957 16-Jan-09 11:36:00 167.142746 6541.25439 63.2382927 2.82692957 16-Jan-09 11:37:00 167.531311 6551.25391 63.3403969 2.82692957 16-Jan-09 11:38:00 167.9198608 6579.67773 63.1707764 2.82692957



### Page 1 of 2

### PI Ops Data Run 5

Tag Name: 1pwrji900 1TSYFI100 1tmsti922m 1tsyai202 Tag Explanation: Unit Load Fuel Flow Inlet Temp Satuator Tag Units: Mwe KCFH oF % H2O 16-Jan-09 11:39:00 167.4830933 6573.37646 62.8652954 2.82692957 16-Jan-09 11:40:00 167.0463257 6550.57813 63.1343727 2.82692957 16-Jan-09 11:41:00 167.2389984 6562.59521 63.4996796 2.82692957 16-Jan-09 11:42:00 167.4533691 6564.99756 63.3282318 2.82692957 16-Jan-09 11:43:00 167.9143677 6570.13184 63.0613098 2.82692957 16-Jan-09 11:44:00 167.9934082 6579.07275 63.0815125 2.82692957 16-Jan-09 11:45:00 168.3523254 6564.85791 63.2153053 2.82692957 16-Jan-09 11:46:00 168.8302002 6560.01758 63.369297 2.82692957 16-Jan-09 11:47:00 168.3196564 6555.90479 63.5386925 2.82692957 16-Jan-09 11:48:00 167.587204 6542.05322 63.6176834 2.82692957 16-Jan-09 11:49:00 167.8499146 6545.53662 63.4624176 2.82692957 16-Jan-09 11:50:00 168.1008606 6542.55127 63.751194 2.82692957 16-Jan-09 11:51:00 168.1458893 6553.03223 63.9039345 2.82692957 16-Jan-09 11:52:00 168.1372223 6565.29932 63.7748146 2.82692957 16-Jan-09 11:53:00 168.536438 6556.18604 63.4103622 2.82692957 16-Jan-09 11:54:00 168.3210449 6547.07275 63.5130272 2.82692957 16-Jan-09 11:55:00 167.6218872 6537.95947 63.6156883 2.82692957 16-Jan-09 11:56:00 167.6221619 6537.25293 63.9570389 2.82692957 16-Jan-09 11:57:00 167.9721375 6530.64355 63.8030472 2.82692957 16-Jan-09 11:58:00 167.9528198 6538.44434 63.7645493 2.82692957 16-Jan-09 11:59:00 168.1585083 6558.33691 64.0725327 2.82692957 16-Jan-09 12:00:00 168.0006866 6558.33691 64.1259232 2.82692957 16-Jan-09 12:01:00 168.3473969 6558.33691 64.9023895 2.82692957 16-Jan-09 12:02:00 168.4600372 6562.53662 64.6970673 2.82692957 16-Jan-09 12:03:00 168.6749725 6571.22607 64.4917374 2.82692957 16-Jan-09 12:04:00 168.6121826 6575.39063 64.6628494 2.82692957 16-Jan-09 12:05:00 167.8395386 6558.19043 64.8784332 2.82692957 16-Jan-09 12:06:00 167.3434448 6543.90186 64.318924 2.82692957 16-Jan-09 12:07:00 167.2344818 6541.24658 64.3805237 2.82692957 16-Jan-09 12:08:00 166.9421539 6527.12939 64.4421158 2.82692957 16-Jan-09 12:09:00 166.7718048 6525.37598 64.5037155 2.82692957 16-Jan-09 12:10:00 167.240097 6536.83838 64.5653152 2.82692957 16-Jan-09 12:11:00 167.6213837 6534.99561 64.626915 2.82692957



### Page 2 of 2

### PI Ops Data Run 6

Plant Information Source: polk-1pisrv Start Time: 01/16/2009 12:20

End Time: 01/16/2009 13:26 Time Interval: 1m

Tag Name: 1pwrji900 1TSYFI100 1tmsti922m 1tsyai202 Tag Explanation: Unit Load Fuel Flow Inlet Temp Satuator Tag Units: Mwe KCFH oF % H2O Run Average: 167.8710571 6516.08692 65.9336523 2.82736543 16-Jan-09 12:20:00 167.6146851 6545.51514 64.6577072 2.82692957 16-Jan-09 12:21:00 167.8386078 6544.78223 64.5037155 2.82692957 16-Jan-09 12:22:00 168.0625153 6544.04883 64.3497238 2.82692957 16-Jan-09 12:23:00 168.2052155 6538.21875 64.7034912 2.82692957 16-Jan-09 12:24:00 167.8820038 6526.94092 64.8055954 2.82692957 16-Jan-09 12:25:00 167.7304382 6534.28613 64.9076996 2.82692957 16-Jan-09 12:26:00 167.3309021 6539.63916 65.5655594 2.82692957 16-Jan-09 12:27:00 167.700119 6522.95557 65.6710663 2.82692957 16-Jan-09 12:28:00 166.8672638 6532.94434 65.9610901 2.82692957 16-Jan-09 12:29:00 166.66539 6534.05078 65.4898758 2.82692957 16-Jan-09 12:30:00 167.854126 6519.46289 65.1279068 2.82692957 16-Jan-09 12:31:00 168.6824341 6547.32422 65.7409363 2.82692957 16-Jan-09 12:32:00 167.8949432 6541.10303 65.7010117 2.82692957 16-Jan-09 12:33:00 167.3377228 6515.31738 65.7908401 2.82692957 16-Jan-09 12:34:00 168.1468964 6521.68115 65.6411285 2.82692957 16-Jan-09 12:35:00 169.1294403 6519.82959 65.7159805 2.82692957 16-Jan-09 12:36:00 168.2575684 6519.65234 66.0015793 2.82692957 16-Jan-09 12:37:00 167.6367188 6515.86377 66.3560333 2.82692957 16-Jan-09 12:38:00 167.1554871 6496.2666 65.6030884 2.82692957 16-Jan-09 12:39:00 167.3088226 6482.86133 65.384758 2.82692957 16-Jan-09 12:40:00 167.2641602 6489.05908 65.6884613 2.82692957 16-Jan-09 12:41:00 166.9417267 6494.52832 66.3018723 2.82692957 16-Jan-09 12:42:00 167.259613 6493.19922 66.4133606 2.82692957 16-Jan-09 12:43:00 167.8989868 6501.81641 66.1854477 2.82692957 16-Jan-09 12:44:00 168.2562103 6518.14258 65.9575272 2.82692957 16-Jan-09 12:45:00 168.6473389 6536.50732 65.7296066 2.82692957 16-Jan-09 12:46:00 168.5527954 6531.93604 65.6497421 2.82692957 16-Jan-09 12:47:00 167.9514618 6500.54199 65.8455963 2.82692957 16-Jan-09 12:48:00 167.7026825 6490.47656 65.7452393 2.82692957 16-Jan-09 12:49:00 167.2933807 6504.55127 65.6448822 2.82692957 16-Jan-09 12:50:00 166.994339 6496.5332 65.8706894 2.82692957 16-Jan-09 12:51:00 167.2846222 6491.58252 65.8706894 2.82692957 16-Jan-09 12:52:00 168.0091553 6515.91162 65.8706894 2.82692957 16-Jan-09 12:53:00 168.7713165 6539.48975 65.7897034 2.82692957



### Page 1 of 2

### PI Ops Data Run 6

Tag Name: 1pwrji900 1TSYFI100 1tmsti922m 1tsyai202 Tag Explanation: Unit Load Fuel Flow Inlet Temp Satuator Tag Units: Mwe KCFH oF % H2O 16-Jan-09 12:54:00 168.7069397 6537.21338 65.3599472 2.82692957 16-Jan-09 12:55:00 168.2550659 6523.09619 66.4799118 2.82692957 16-Jan-09 12:56:00 168.0397797 6527.49902 66.2757034 2.82692957 16-Jan-09 12:57:00 168.1793671 6530.96436 66.0714951 2.82692957 16-Jan-09 12:58:00 167.9970093 6543.27881 65.8732529 2.82692957 16-Jan-09 12:59:00 167.8085175 6558.08643 66.0272522 2.82692957 16-Jan-09 13:00:00 168.1181335 6516.90186 66.1812515 2.82692957 16-Jan-09 13:01:00 167.6589966 6493.08008 65.5865173 2.82692957 16-Jan-09 13:02:00 167.8914795 6527.10791 65.709816 2.82692957 16-Jan-09 13:03:00 169.1100769 6539.8623 65.8583145 2.82692957 16-Jan-09 13:04:00 168.22995 6515.29492 66.7176514 2.82692957 16-Jan-09 13:05:00 168.0678558 6510.93115 66.5328674 2.82692957 16-Jan-09 13:06:00 167.9949188 6516.58643 65.688324 2.82692957 16-Jan-09 13:07:00 168.2786407 6509.86377 66.2963257 2.82692957 16-Jan-09 13:08:00 168.5623627 6503.14111 66.3686066 2.82703304 16-Jan-09 13:09:00 168.4671783 6505.5166 66.2146149 2.82719231 16-Jan-09 13:10:00 168.3383179 6511.59131 66.4302063 2.82735157 16-Jan-09 13:11:00 167.1766968 6498.28711 66.183815 2.82751083 16-Jan-09 13:12:00 167.0695038 6487.87207 66.7279205 2.8276701 16-Jan-09 13:13:00 166.971283 6482.25098 67.0359039 2.82782936 16-Jan-09 13:14:00 167.0433197 6481.37598 66.7947769 2.82798862 16-Jan-09 13:15:00 167.1153717 6493.32422 66.3365555 2.82814789 16-Jan-09 13:16:00 167.1874084 6499.9248 66.1153717 2.82830715 16-Jan-09 13:17:00 168.4721375 6499.43604 66.0127106 2.82846665 16-Jan-09 13:18:00 168.0146637 6501.64795 65.9100418 2.82862592 16-Jan-09 13:19:00 167.4971161 6506.51904 66.0606155 2.82878518 16-Jan-09 13:20:00 167.368576 6516.66357 66.729248 2.82894444 16-Jan-09 13:21:00 169.1936798 6525.0498 67.0068207 2.82910371 16-Jan-09 13:22:00 167.2852783 6506.63477 66.8014984 2.82926297 16-Jan-09 13:23:00 168.6559143 6511.82275 66.5961761 2.82942224 16-Jan-09 13:24:00 168.6040955 6523.05029 66.6522217 2.8295815 16-Jan-09 13:25:00 168.3111115 6522.48779 66.3467407 2.82974076 16-Jan-09 13:26:00 167.5609894 6504.44092 66.3299332 2.82990003



### Page 2 of 2

## APPENDIX D

FUEL ANALYSISDate/time Date/time 12/16/08 8:00
ELEMENT Pi Tag CAL. GAS MS Actual MS Normalized Adjustment
H2 1ASHYI015 36.00 36.20 36.22 1.006 N2 1ASHYI016 3.15 3.13 3.13 0.994 CH4 1ASHYI018 0.0336 0.0328 0.0328 0.977 CO 1ASHYI021 44.14 43.90 43.93 0.995 H2S 1ASHYI019 0.6010 0.6216 0.6220 1.00 CO2 1ASHYI022 15.00 15.00 15.01 1.001 COS 1ASHYI020 0.0300 0.0204 0.0204 1.00 AR 1ASHYI017 1.05 1.03 1.03 0.982 Subtotal (Dry) 100.00 99.93 100.00 1.000 H2O 1TSYAI202 Total (Moist) Mole Wt (Moist) Flow (KSCFH) 1TSYFI100 Mole Wt (Dry) HHV-Dry (BTU/SCF) HHV-Moist (BTU/SCF) HHV (MMBTU/Hr) LHV (BTU/SCF) LHV (MMTU/Hr) CALIBRATION CHECK AND ADJUSTMENT FACTORS1/15/09 11:01 1/15/09 12:45 1/15/09 12:07 1/15/09 13:51
Raw Data Adjusted Data Normalized & Adjusted Raw Data Adjusted Data Normalized & Adjusted
33.40 33.61 32.96 33.38 33.59 32.86

3.99 3.96 3.93 3.88 3.86 3.82
0.03 0.03 0.03 0.03 0.03 0.03
46.11 45.90 45.50 46.24 46.02 45.52

0.01 0.01 0.01 0.02 0.02 0.01
14.49 14.50 14.30 14.51 14.52 14.28

0.01 0.01 0.01 0.01 0.01 0.01
0.84 0.82 0.82 0.83 0.81 0.82
98.88 98.84 97.57 98.89 98.85 97.36

2.43 2.43 2.43 2.64 2.64 2.64 100.00 100.00

21.59 21.59 6505 6402 6525 6422 21.68 21.69 259.5 259.8 253.2 253.0 1621 1624 236.7 236.5 1516 1519 Run 1 Run 21/15/09 14:37 1/15/09 15:43 1/15/09 15:43 1/15/09 16:59
Raw Data Adjusted Data Normalized & Adjusted Raw Data Adjusted Data Normalized & Adjusted
33.36 33.56 32.82 33.35 33.55 32.78

3.89 3.86 3.82 3.97 3.95 3.90
0.03 0.03 0.03 0.03 0.03 0.03
46.12 45.90 45.37 45.93 45.72 45.16

0.02 0.02 0.02 0.02 0.02 0.02
14.62 14.63 14.38 14.77 14.78 14.52

0.01 0.01 0.01 0.01 0.01 0.01
0.83 0.82 0.82 0.84 0.82 0.82
98.86 98.83 97.26 98.92 98.88 97.25

2.74 2.74 2.74 2.75 2.75 2.75 100.00 100.00

21.61 21.64 6550 6444 6568 6456 21.71 21.74 259.4 258.7 252.3 251.5 1626 1624 235.9 235.2 1520 1518 Run 3 Run 41/16/09 9:38 1/16/09 11:05 1/16/09 10:47 1/16/09 12:11
Raw Data Adjusted Data Normalized & Adjusted Raw Data Adjusted Data Normalized & Adjusted
33.61 33.82 32.96 33.72 33.93 33.09

4.19 4.17 4.11 4.08 4.05 4.00
0.03 0.03 0.03 0.03 0.03 0.03
45.62 45.41 44.73 45.45 45.23 44.61

0.01 0.01 0.01 0.01 0.01 0.01
14.78 14.79 14.49 14.86 14.87 14.58

0.01 0.01 0.01 0.01 0.01 0.01
0.85 0.84 0.84 0.85 0.83 0.83
99.11 99.07 97.17 99.00 98.96 97.17

2.83 2.83 2.83 2.83 2.83 2.83 100.00 100.00

21.58 21.56 6579 6476 6563 6464 21.68 21.66 258.0 258.1 250.7 250.8 1624 1621 234.2 234.2 1517 1514 Run 5 Run 61/16/09 12:20 1/16/09 13:26
Raw Data Adjusted Data Normalized & Adjusted
33.84 34.05 33.25

3.99 3.96 3.92
0.03 0.03 0.03
45.55 45.34 44.75

0.01 0.01 0.01
14.63 14.64 14.38

0.01 0.01 0.01
0.84 0.83 0.83
98.90 98.87 97.17

2.83 2.83 2.83 100.00

21.49 6516 6428 21.59 259.0 251.7 1618 235.1 1511 Run 7

## APPENDIX E

CEMS DATA

### CEMS Data

Date Time SO21 NOX1 CO21 OXY1 FLO1 01/15/2009 11:01 42.16 18.7 8.6 10.8 813.3 01/15/2009 11:02 42.21 18.7 8.6 10.8 810.9 01/15/2009 11:03 42.11 18.5 8.7 10.8 793.7 01/15/2009 11:04 42.03 18.4 8.6 10.8 789.2 01/15/2009 11:05 41.77 18.1 8.6 10.8 798.6 01/15/2009 11:06 41.97 18 8.6 10.7 797 01/15/2009 11:07 41.92 18.2 8.6 10.8 784.9 01/15/2009 11:08 41.77 18.3 8.6 10.7 788.7 01/15/2009 11:09 41.78 18 8.7 10.7 797.1 01/15/2009 11:10 41.74 17.7 8.7 10.7 802.6 01/15/2009 11:11 41.78 17.9 8.7 10.7 805.1 01/15/2009 11:12 42.1 18.1 8.7 10.7 798.5 01/15/2009 11:13 42.57 18.1 8.6 10.8 796.3 01/15/2009 11:14 42.77 18.6 8.7 10.8 796.3 01/15/2009 11:15 42.63 18.6 8.6 10.8 801 01/15/2009 11:16 42.85 18.6 8.6 10.8 787.4 01/15/2009 11:17 42.62 18.8 8.6 10.8 791.6 01/15/2009 11:18 42.23 18.9 8.6 10.8 789.7 01/15/2009 11:19 42.29 18.8 8.6 10.8 787.7 01/15/2009 11:20 42.26 18.6 8.6 10.8 790.7 01/15/2009 11:21 42.04 18.7 8.6 10.8 799.6 01/15/2009 11:22 41.81 18.7 8.6 10.8 803.4 01/15/2009 11:23 42.02 18.7 8.6 10.8 789.3 01/15/2009 11:24 42.32 18.8 8.6 10.8 802.9 01/15/2009 11:25 42.39 19 8.6 10.8 786.1 01/15/2009 11:26 42.54 18.9 8.6 10.9 791.5 01/15/2009 11:27 42.1 19 8.6 10.8 795.7 01/15/2009 11:28 42.24 19 8.6 10.8 797.4 01/15/2009 11:29 42.67 18.8 8.6 10.8 796.9 01/15/2009 11:30 42.62 18.6 8.6 10.8 800.8 01/15/2009 11:31 42.78 18.9 8.6 10.8 802.6 01/15/2009 11:32 42.68 19.4 8.6 10.8 796.9 01/15/2009 11:33 42.63 19.6 8.6 10.9 796.1 01/15/2009 11:34 42.53 19.6 8.6 10.9 792 01/15/2009 11:35 42.38 19.2 8.6 10.9 800.4 01/15/2009 11:36 42.37 18.9 8.6 10.9 801.5 01/15/2009 11:37 42.61 18.9 8.6 10.9 792.6 01/15/2009 11:38 42.59 19.4 8.6 10.9 793 01/15/2009 11:39 42.81 18.8 8.6 10.8 795.8 01/15/2009 11:40 42.57 18.4 8.6 10.9 795.8 01/15/2009 11:41 42.33 18.8 8.6 10.9 796.4 Run 1

Page 1 of 13

### CEMS Data

01/15/2009 11:42 42.39 19.1 8.6 10.9 806.2 01/15/2009 11:43 42.28 19.5 8.6 10.9 795.8 01/15/2009 11:44 42.15 19.2 8.6 10.9 798.5 01/15/2009 11:45 41.98 19 8.6 10.9 795 01/15/2009 11:46 42.16 18.9 8.6 10.9 793.8 01/15/2009 11:47 42.09 19 8.6 10.9 789.9 01/15/2009 11:48 41.79 19.4 8.6 10.9 814.2 01/15/2009 11:49 42.02 19.4 8.6 10.9 801.4 01/15/2009 11:50 41.81 19.3 8.6 10.9 807.2 01/15/2009 11:51 42.39 19.2 8.6 10.9 797.6 01/15/2009 11:52 42.28 19.5 8.7 10.9 795.2 01/15/2009 11:53 42.34 19.8 8.7 10.9 794 01/15/2009 11:54 41.97 19.4 8.6 10.9 794.2 01/15/2009 11:55 42.09 18.8 8.6 10.9 795 01/15/2009 11:56 42.21 18.9 8.7 10.9 789.5 01/15/2009 11:57 42.31 18.9 8.6 10.9 794.2 01/15/2009 11:58 42.24 19.1 8.6 10.9 795.5 01/15/2009 11:59 42.32 19 8.6 10.9 798.1 01/15/2009 12:00 42.42 18.5 8.6 10.8 797.8 01/15/2009 12:01 42.66 18.8 8.6 10.9 793.1 01/15/2009 12:02 42.33 18.9 8.6 10.8 791.5 01/15/2009 12:03 42.5 19 8.6 10.9 798.5 01/15/2009 12:04 42.44 18.9 8.6 10.8 786.2 01/15/2009 12:05 42.3 18.8 8.6 10.9 789.4 01/15/2009 12:06 42.37 18.7 8.6 10.9 793.7 01/15/2009 12:07 42.49 18.7 8.6 10.8 788.6 42.28 18.83 8.61 10.84 796.14

Date Time SO21 NOX1 CO21 OXY1 FLO1 01/15/2009 12:45 41.47 19.5 8.6 10.9 800.1 01/15/2009 12:46 41.41 19.6 8.6 10.9 802.3 01/15/2009 12:47 41.44 19.3 8.6 10.9 804.4 01/15/2009 12:48 41.56 19.5 8.6 10.9 808.3 01/15/2009 12:49 41.81 19.4 8.6 10.9 804 01/15/2009 12:50 41.51 19.1 8.6 10.9 801.8 01/15/2009 12:51 41.17 19.1 8.6 10.9 798.9 01/15/2009 12:52 41.53 19.2 8.6 10.9 802.2 01/15/2009 12:53 41.46 19.4 8.6 10.9 799.2 Run 2

Page 2 of 13

### CEMS Data

01/15/2009 12:54 41.79 19.5 8.6 10.9 803.9 01/15/2009 12:55 41.85 19.4 8.6 10.9 795.2 01/15/2009 12:56 41.87 19.5 8.6 10.9 781 01/15/2009 12:57 42.07 19.2 8.6 10.9 790.8 01/15/2009 12:58 42 19.2 8.6 10.9 793.3 01/15/2009 12:59 42.1 18.8 8.6 10.8 791.1 01/15/2009 13:00 41.79 18.5 8.6 10.9 793.2 01/15/2009 13:01 41.55 18.8 8.6 10.9 794.3 01/15/2009 13:02 41.65 18.9 8.6 10.8 795 01/15/2009 13:03 41.64 19 8.6 10.8 795.8 01/15/2009 13:04 41.85 18.6 8.6 10.8 798.2 01/15/2009 13:05 42.05 18.8 8.6 10.8 798.4 01/15/2009 13:06 42.1 18.9 8.6 10.9 801 01/15/2009 13:07 41.89 18.5 8.6 10.9 802.8 01/15/2009 13:08 42.14 18.5 8.6 10.8 786.7 01/15/2009 13:09 42.02 18.6 8.6 10.8 811.7 01/15/2009 13:10 41.96 18.9 8.6 10.8 792.7 01/15/2009 13:11 41.85 18.6 8.6 10.8 798.6 01/15/2009 13:12 42 18.6 8.6 10.8 800.4 01/15/2009 13:13 42.08 18.6 8.6 10.8 796.8 01/15/2009 13:14 41.88 18.5 8.6 10.8 794 01/15/2009 13:15 41.81 18.3 8.6 10.8 794 01/15/2009 13:16 42.23 18 8.6 10.8 788.4 01/15/2009 13:17 42.19 18.1 8.6 10.8 789.1 01/15/2009 13:18 42.62 18.4 8.6 10.8 789.8 01/15/2009 13:19 42.41 18.3 8.6 10.8 788.6 01/15/2009 13:20 42.13 18.1 8.6 10.8 784.2 01/15/2009 13:21 42.39 18.3 8.6 10.8 791.5 01/15/2009 13:22 42.07 18.5 8.6 10.8 803.5 01/15/2009 13:23 42.17 18.4 8.6 10.9 804.6 01/15/2009 13:24 42 18.2 8.5 10.8 794.9 01/15/2009 13:25 41.91 18.1 8.5 10.8 783.8 01/15/2009 13:26 42.38 18.1 8.5 10.8 795.1 01/15/2009 13:27 42.48 18.1 8.5 10.8 797.8 01/15/2009 13:28 42.94 17.9 8.5 10.8 801.3 01/15/2009 13:29 42.74 18 8.5 10.8 801.6 01/15/2009 13:30 42.92 18.1 8.5 10.8 805.8 01/15/2009 13:31 42.56 17.9 8.5 10.8 791 01/15/2009 13:32 42.73 17.9 8.5 10.8 785.8 01/15/2009 13:33 42.77 18.1 8.5 10.8 792.2 01/15/2009 13:34 42.73 18.2 8.5 10.8 794.5 01/15/2009 13:35 42.6 18.3 8.5 10.8 796.1 01/15/2009 13:36 42.72 18 8.5 10.8 798.1

Page 3 of 13

### CEMS Data

01/15/2009 13:37 42.64 17.8 8.5 10.8 793.8 01/15/2009 13:38 42.47 18.1 8.5 10.8 791 01/15/2009 13:39 42.68 18 8.5 10.8 798.1 01/15/2009 13:40 42.82 17.9 8.5 10.8 799.7 01/15/2009 13:41 42.97 17.9 8.5 10.8 797.1 01/15/2009 13:42 42.95 18 8.5 10.8 797.6 01/15/2009 13:43 42.96 17.7 8.5 10.8 798.1 01/15/2009 13:44 42.66 17.6 8.5 10.8 796.3 01/15/2009 13:45 42.83 17.6 8.5 10.8 794.4 01/15/2009 13:46 43.15 17.6 8.5 10.8 797.1 01/15/2009 13:47 43.13 17.5 8.5 10.8 799.1 01/15/2009 13:48 43.16 17.7 8.5 10.8 789.7 01/15/2009 13:49 43.35 17.4 8.5 10.7 787.7 01/15/2009 13:50 43.15 17.3 8.6 10.8 785.4 01/15/2009 13:51 43.2 17.7 8.6 10.8 794.9 42.26 18.43 8.56 10.83 795.94

Date Time SO21 NOX1 CO21 OXY1 FLO1 01/15/2009 14:37 44.23 17.6 8.6 10.8 794.7 01/15/2009 14:38 44.51 18.1 8.6 10.8 793.3 01/15/2009 14:39 44.19 17.8 8.6 10.8 795.8 01/15/2009 14:40 44.32 17.6 8.6 10.8 792.7 01/15/2009 14:41 44.31 17.7 8.6 10.8 789.3 01/15/2009 14:42 44.21 17.7 8.6 10.8 790.4 01/15/2009 14:43 44.01 17.7 8.6 10.8 792.5 01/15/2009 14:44 44.1 17.8 8.6 10.8 805.9 01/15/2009 14:45 44.25 17.7 8.6 10.8 802.7 01/15/2009 14:46 44 17.7 8.6 10.8 808.3 01/15/2009 14:47 43.91 17.9 8.6 10.8 806.2 01/15/2009 14:48 43.91 17.9 8.6 10.8 805 01/15/2009 14:49 44.31 17.8 8.6 10.8 801.5 01/15/2009 14:50 44.34 17.9 8.6 10.8 792.6 01/15/2009 14:51 44.19 17.7 8.6 10.8 793.5 01/15/2009 14:52 44.16 17.7 8.6 10.8 794.9 Run 3

Page 4 of 13

### CEMS Data

01/15/2009 14:53 44.06 17.9 8.6 10.8 795.9 01/15/2009 14:54 43.95 17.8 8.6 10.8 795.5 01/15/2009 14:55 44.08 17.7 8.6 10.8 801.5 01/15/2009 14:56 43.74 17.8 8.6 10.8 799.3 01/15/2009 14:57 43.61 18.1 8.6 10.8 792.1 01/15/2009 14:58 43.5 18.1 8.6 10.8 792.2 01/15/2009 14:59 43.61 17.9 8.6 10.7 795.9 01/15/2009 15:00 43.57 17.4 8.6 10.7 798.3 01/15/2009 15:01 43.39 17.4 8.6 10.8 803 01/15/2009 15:02 43.65 17.3 8.6 10.8 802.6 01/15/2009 15:03 43.82 17.1 8.6 10.7 804.2 01/15/2009 15:04 44.06 17.2 8.6 10.7 797 01/15/2009 15:05 44.16 17.4 8.6 10.8 793.8 01/15/2009 15:06 43.97 17.5 8.6 10.8 797.2 01/15/2009 15:07 43.86 17.5 8.6 10.8 798.9 01/15/2009 15:08 43.98 17.5 8.6 10.8 799.1 01/15/2009 15:09 44.11 17.2 8.6 10.7 797.2 01/15/2009 15:10 44.13 17 8.6 10.8 788.6 01/15/2009 15:11 44.35 17.4 8.6 10.8 799.7 01/15/2009 15:12 44.66 17.7 8.6 10.8 803.2 01/15/2009 15:13 44.72 17.7 8.6 10.8 799.4 01/15/2009 15:14 44.74 17.9 8.6 10.8 796 01/15/2009 15:15 44.48 17.9 8.6 10.8 798 01/15/2009 15:16 44.42 18 8.6 10.8 793.6 01/15/2009 15:17 44.16 18.2 8.6 10.8 787.1 01/15/2009 15:18 44.1 18.3 8.6 10.8 790.5 01/15/2009 15:19 43.81 18.2 8.6 10.8 796.2 01/15/2009 15:20 43.96 18.2 8.6 10.8 794.2 01/15/2009 15:21 43.71 18.1 8.6 10.8 797.7 01/15/2009 15:22 44.05 17.9 8.6 10.8 790.1 01/15/2009 15:23 44.17 18.1 8.7 10.8 790.2 01/15/2009 15:24 43.87 18 8.6 10.8 794 01/15/2009 15:25 43.9 17.8 8.6 10.8 781.8 01/15/2009 15:26 43.76 17.9 8.6 10.8 786.2 01/15/2009 15:27 43.49 17.9 8.6 10.8 801.6 01/15/2009 15:28 43.59 17.9 8.6 10.8 796.8 01/15/2009 15:29 43.42 18 8.6 10.8 792.2 01/15/2009 15:30 43.48 18.1 8.6 10.8 801.4 01/15/2009 15:31 43.35 18 8.6 10.8 799.5 01/15/2009 15:32 43.32 18.1 8.7 10.8 801.1 01/15/2009 15:33 43.48 18.1 8.7 10.8 799.9 01/15/2009 15:34 43.57 17.8 8.6 10.8 792.2 01/15/2009 15:35 43.74 17.7 8.6 10.8 789.1

Page 5 of 13

### CEMS Data

01/15/2009 15:36 43.91 17.8 8.6 10.8 794 01/15/2009 15:37 43.82 17.7 8.6 10.8 793.9 01/15/2009 15:38 44.08 17.8 8.6 10.8 796.1 01/15/2009 15:39 43.94 17.7 8.7 10.7 798 01/15/2009 15:40 43.55 17.4 8.7 10.8 797.8 01/15/2009 15:41 43.65 17.7 8.7 10.8 787.2 01/15/2009 15:42 44.04 17.7 8.7 10.8 796.9 01/15/2009 15:43 43.96 17.8 8.7 10.8 793.4 43.96 17.77 8.61 10.79 796.128358

Date Time SO21 NOX1 CO21 OXY1 FLO1 01/15/2009 15:53 43.8 17.7 8.7 10.8 789.4 01/15/2009 15:54 43.74 17.6 8.7 10.8 784.5 01/15/2009 15:55 43.57 17.5 8.7 10.8 799.6 01/15/2009 15:56 43.65 17.7 8.7 10.8 803.1 01/15/2009 15:57 43.55 17.5 8.7 10.8 797.3 01/15/2009 15:58 43.55 17.6 8.6 10.8 800.6 01/15/2009 15:59 43.51 17.6 8.7 10.8 803.7 01/15/2009 16:00 43.73 17.4 8.7 10.7 797.3 01/15/2009 16:01 44.11 17.4 8.7 10.8 804.2 01/15/2009 16:02 43.86 17.5 8.7 10.8 806.1 01/15/2009 16:03 44.16 17.3 8.6 10.8 800.9 01/15/2009 16:04 43.9 17.1 8.6 10.8 796.3 01/15/2009 16:05 43.89 17.2 8.7 10.8 790.8 01/15/2009 16:06 43.95 17.2 8.7 10.8 783.3 01/15/2009 16:07 43.88 17.2 8.7 10.8 793.9 01/15/2009 16:08 43.94 17.4 8.7 10.8 788.6 01/15/2009 16:09 43.68 17.3 8.6 10.8 787.9 01/15/2009 16:10 43.56 17.4 8.7 10.8 789 Run 4

Page 6 of 13

### CEMS Data

01/15/2009 16:11 43.59 17.5 8.7 10.7 800.9 01/15/2009 16:12 43.6 17.5 8.7 10.8 785.9 01/15/2009 16:13 43.82 17.5 8.7 10.8 805.8 01/15/2009 16:14 43.52 17.5 8.7 10.8 794.7 01/15/2009 16:15 43.85 17.6 8.7 10.8 792.5 01/15/2009 16:16 44.01 17.3 8.7 10.7 798.9 01/15/2009 16:17 44.1 17.3 8.7 10.8 798 01/15/2009 16:18 43.96 17.3 8.7 10.7 794.4 01/15/2009 16:19 43.91 17.1 8.7 10.7 791 01/15/2009 16:20 43.95 17 8.7 10.7 796.6 01/15/2009 16:21 43.66 17 8.7 10.7 793.7 01/15/2009 16:22 43.46 17.1 8.7 10.7 791.8 01/15/2009 16:23 43.72 17.1 8.7 10.7 792.7 01/15/2009 16:24 43.41 16.9 8.7 10.7 790.4 01/15/2009 16:25 43.58 17 8.7 10.7 791.1 01/15/2009 16:26 43.82 17 8.7 10.7 793.3 01/15/2009 16:27 44 17 8.7 10.7 792.2 01/15/2009 16:28 44.5 17.1 8.7 10.7 784.6 01/15/2009 16:29 45.22 16.9 8.7 10.7 793.8 01/15/2009 16:30 44.27 16.7 8.7 10.7 792.3 01/15/2009 16:31 44.52 16.9 8.7 10.7 786.9 01/15/2009 16:32 44.4 17.1 8.7 10.8 783.7 01/15/2009 16:33 44.33 17.4 8.7 10.8 787.4 01/15/2009 16:34 44.24 17.7 8.7 10.8 796.8 01/15/2009 16:35 43.92 17.6 8.7 10.8 797.2 01/15/2009 16:36 44.21 17.6 8.7 10.7 794.8 01/15/2009 16:37 44.2 17.5 8.7 10.8 792.6 01/15/2009 16:38 44 17.4 8.7 10.8 797.7 01/15/2009 16:39 43.98 17.6 8.7 10.8 792.7 01/15/2009 16:40 43.85 17.5 8.7 10.8 795.3 01/15/2009 16:41 44.01 17.6 8.7 10.8 793.2 01/15/2009 16:42 44.05 17.6 8.7 10.8 792.7 01/15/2009 16:43 43.75 17.5 8.7 10.7 793.4 01/15/2009 16:44 43.44 17.5 8.7 10.7 805.4 01/15/2009 16:45 43.74 17.4 8.7 10.8 794.3 01/15/2009 16:46 43.83 17.3 8.7 10.7 788.3 01/15/2009 16:47 43.74 17.4 8.7 10.8 791.9 01/15/2009 16:48 43.82 17.3 8.7 10.8 795.3 01/15/2009 16:49 44.07 17.4 8.7 10.8 793.4 01/15/2009 16:50 43.55 17.4 8.7 10.8 807.5 01/15/2009 16:51 43.79 17.5 8.7 10.8 783.3 01/15/2009 16:52 43.53 17.5 8.7 10.8 798.1 01/15/2009 16:53 43.65 17.3 8.7 10.8 782.7

Page 7 of 13

### CEMS Data

01/15/2009 16:54 44.02 17.3 8.7 10.8 786.8 01/15/2009 16:55 43.92 17.6 8.7 10.8 792 01/15/2009 16:56 43.8 17.1 8.7 10.8 806.6 01/15/2009 16:57 43.93 17.3 8.7 10.8 796 01/15/2009 16:58 44.11 17.5 8.7 10.8 797.1 01/15/2009 16:59 43.76 17.3 8.7 10.7 794.4 43.88 17.34 8.69 10.77 794.16 795.41

Date Time SO21 NOX1 CO21 OXY1 FLO1 01/16/2009 9:38 39.04 17 8.7 10.7 787.9 01/16/2009 9:39 38.84 16.9 8.7 10.7 784.8 01/16/2009 9:40 39.19 16.8 8.7 10.7 779 01/16/2009 9:41 39.06 16.7 8.7 10.7 790.3 01/16/2009 9:42 39.14 16.7 8.7 10.7 796.4 01/16/2009 9:43 39.45 16.6 8.7 10.7 805.2 01/16/2009 9:44 39.22 16.6 8.7 10.7 795.8 01/16/2009 9:45 39.44 16.8 8.7 10.7 794.2 01/16/2009 9:46 39.3 17.1 8.7 10.7 789 01/16/2009 9:47 39.39 16.8 8.7 10.7 782.9 01/16/2009 9:48 39.45 16.5 8.7 10.7 786.5 01/16/2009 9:49 39.65 16.6 8.7 10.7 785.5 01/16/2009 9:50 39.89 16.4 8.7 10.7 786.2 01/16/2009 9:51 39.42 16.4 8.7 10.7 791.9 01/16/2009 9:52 39.47 16.6 8.7 10.7 794 01/16/2009 9:53 39.27 16.8 8.7 10.7 797.5 01/16/2009 9:54 39.24 16.6 8.7 10.7 798 01/16/2009 9:55 39.53 16.7 8.7 10.7 786.4 01/16/2009 9:56 39.64 16.7 8.7 10.7 797.4 01/16/2009 9:57 39.37 16.8 8.7 10.7 795.5 01/16/2009 9:58 39.44 16.9 8.7 10.7 795.8 Run 5

Page 8 of 13

### CEMS Data

01/16/2009 9:59 39.68 16.7 8.7 10.7 789.5 01/16/2009 10:00 39.51 16.5 8.7 10.7 790.6 01/16/2009 10:01 39.4 16.8 8.7 10.7 788.2 01/16/2009 10:02 39.4 16.8 8.7 10.7 804.1 01/16/2009 10:03 39.36 16.6 8.7 10.7 790.5 01/16/2009 10:04 39.14 16.6 8.7 10.7 794.2 01/16/2009 10:05 39.47 16.5 8.7 10.7 792.5 01/16/2009 10:06 39.27 16.6 8.7 10.7 792.5 01/16/2009 10:07 39.46 16.5 8.7 10.7 793.5 01/16/2009 10:08 39.49 16.8 8.7 10.7 794.9 01/16/2009 10:09 39.47 16.9 8.7 10.7 794.5 01/16/2009 10:10 39.37 16.4 8.7 10.7 801.4 01/16/2009 10:11 39.61 16.6 8.7 10.7 793.9 01/16/2009 10:12 39.36 16.7 8.7 10.7 786.1 01/16/2009 10:13 39.56 16.7 8.7 10.7 783.6 01/16/2009 10:14 39.51 16.9 8.7 10.7 781.8 01/16/2009 10:15 39.79 16.7 8.7 10.7 796.7 01/16/2009 10:16 39.44 16.5 8.7 10.7 799.6 01/16/2009 10:17 39.7 16.6 8.7 10.7 799.3 01/16/2009 10:18 39.26 16.9 8.7 10.7 793.7 01/16/2009 10:19 38.96 16.8 8.7 10.7 789.1 01/16/2009 10:20 39.35 16.3 8.7 10.6 783.3 01/16/2009 10:21 39.17 16.1 8.7 10.6 786.1 01/16/2009 10:22 39.19 16.5 8.7 10.7 806 01/16/2009 10:23 39.35 16.5 8.7 10.7 795.4 01/16/2009 10:24 39.41 16.7 8.7 10.7 786.4 01/16/2009 10:25 39.61 16.7 8.7 10.7 788.9 01/16/2009 10:26 39.59 16.8 8.7 10.7 789.2 01/16/2009 10:27 39.59 17 8.7 10.7 789.2 01/16/2009 10:28 39.62 16.7 8.7 10.7 783.8 01/16/2009 10:29 39.56 16.6 8.7 10.7 791 01/16/2009 10:30 39.44 16.5 8.7 10.7 789.6 01/16/2009 10:31 39.17 16.4 8.7 10.7 791.1 01/16/2009 10:32 39.06 16.5 8.7 10.7 793.6 01/16/2009 10:33 39.52 17 8.7 10.7 797.2 01/16/2009 10:34 39.34 16.6 8.7 10.7 791.3 01/16/2009 10:35 39.51 16.5 8.7 10.7 782.3 01/16/2009 10:36 39.49 16.5 8.7 10.7 783.9 01/16/2009 10:37 39.4 16.7 8.6 10.7 784 01/16/2009 10:38 39.6 16.9 8.7 10.7 788.7 01/16/2009 10:39 39.82 17 8.7 10.7 794.4 01/16/2009 10:40 39.69 16.8 8.6 10.6 792.5 01/16/2009 10:41 39.38 16.1 8.6 10.6 793.8

Page 9 of 13

### CEMS Data

01/16/2009 10:42 39.31 16.2 8.6 10.6 791.8 01/16/2009 10:43 39.59 16.3 8.6 10.7 786.8 01/16/2009 10:44 39.72 16.5 8.6 10.6 783.2 01/16/2009 10:45 39.33 16.3 8.6 10.7 784.6 01/16/2009 10:46 39.45 16.3 8.6 10.7 790.7 01/16/2009 10:47 39.19 16.2 8.6 10.6 785.1 39.415714 16.63 8.687 10.69 791.061429 47463686

Date Time SO21 NOX1 CO21 OXY1 FLO1 01/16/2009 11:05 39.15 17 8.6 10.7 790.8 01/16/2009 11:06 39.32 16.8 8.6 10.7 795.3 01/16/2009 11:07 39.23 16.8 8.6 10.7 801.1 01/16/2009 11:08 39.28 16.9 8.6 10.7 788.3 01/16/2009 11:09 39.53 17 8.6 10.7 786.9 01/16/2009 11:10 39.42 16.7 8.6 10.6 788.4 01/16/2009 11:11 39.37 16.3 8.6 10.6 792 01/16/2009 11:12 39.5 16.6 8.6 10.7 804.6 01/16/2009 11:13 39.5 16.8 8.6 10.7 786.3 01/16/2009 11:14 39.66 16.8 8.6 10.7 785.3 01/16/2009 11:15 39.58 16.9 8.6 10.7 782.5 01/16/2009 11:16 39.57 16.9 8.6 10.7 781.3 01/16/2009 11:17 39.58 16.8 8.6 10.7 789.3 01/16/2009 11:18 39.45 17 8.6 10.8 792.1 01/16/2009 11:19 39.28 16.9 8.6 10.7 781.8 01/16/2009 11:20 39.24 16.9 8.6 10.7 783.2 01/16/2009 11:21 39.06 16.9 8.6 10.7 786.1 01/16/2009 11:22 39 16.7 8.6 10.7 789.1 01/16/2009 11:23 39.12 16.9 8.6 10.7 794.4 01/16/2009 11:24 39.09 17 8.6 10.7 792.6 01/16/2009 11:25 39.25 16.7 8.6 10.7 775.7 Run 6

Page 10 of 13

### CEMS Data

01/16/2009 11:26 38.92 16.8 8.6 10.7 787.1 01/16/2009 11:27 39.05 17 8.6 10.7 790.5 01/16/2009 11:28 39.08 16.9 8.6 10.7 790.9 01/16/2009 11:29 39.19 17.2 8.6 10.7 788.8 01/16/2009 11:30 39.03 17.2 8.6 10.7 792 01/16/2009 11:31 39.02 16.6 8.6 10.7 793.6 01/16/2009 11:32 39.16 16.9 8.7 10.7 797.3 01/16/2009 11:33 39.39 16.9 8.7 10.7 797.9 01/16/2009 11:34 39.16 16.8 8.7 10.7 790 01/16/2009 11:35 39.1 16.9 8.6 10.8 784.5 01/16/2009 11:36 38.99 17.1 8.6 10.8 789.5 01/16/2009 11:37 38.89 17.1 8.6 10.7 793.5 01/16/2009 11:38 38.83 16.9 8.6 10.7 790.2 01/16/2009 11:39 38.89 17 8.6 10.7 796.6 01/16/2009 11:40 38.67 16.6 8.6 10.7 787.2 01/16/2009 11:41 38.38 16.6 8.6 10.7 777.8 01/16/2009 11:42 38.56 17.1 8.6 10.8 792.7 01/16/2009 11:43 38.71 17.2 8.6 10.7 802.2 01/16/2009 11:44 38.6 17 8.6 10.7 801.9 01/16/2009 11:45 38.78 17.3 8.6 10.7 796.8 01/16/2009 11:46 38.5 17.1 8.6 10.8 792.2 01/16/2009 11:47 38.44 17.1 8.6 10.8 795 01/16/2009 11:48 38.43 17.5 8.6 10.7 795.5 01/16/2009 11:49 38.55 17.2 8.6 10.7 801.3 01/16/2009 11:50 38.75 17.2 8.6 10.7 800.7 01/16/2009 11:51 38.56 17.3 8.6 10.7 797.2 01/16/2009 11:52 38.63 17.5 8.6 10.8 793.3 01/16/2009 11:53 38.77 17.6 8.6 10.8 783.2 01/16/2009 11:54 38.49 17.6 8.6 10.7 783.9 01/16/2009 11:55 38.64 17.5 8.6 10.7 781.2 01/16/2009 11:56 38.69 17.6 8.6 10.8 789.3 01/16/2009 11:57 38.48 17.9 8.6 10.8 791.2 01/16/2009 11:58 38.53 17.9 8.6 10.7 785.7 01/16/2009 11:59 38.27 17.4 8.6 10.7 783.4 01/16/2009 12:00 38.47 17.1 8.6 10.7 784.9 01/16/2009 12:01 38.61 17.1 8.6 10.7 789.5 01/16/2009 12:02 37.88 17.5 8.6 10.7 789.3 01/16/2009 12:03 38.09 17.4 8.6 10.7 787.3 01/16/2009 12:04 38.43 17.2 8.6 10.7 787.4 01/16/2009 12:05 38.46 17 8.6 10.7 787.1 01/16/2009 12:06 38.37 17.2 8.6 10.8 788 01/16/2009 12:07 38.49 17.5 8.6 10.8 783.3 01/16/2009 12:08 38.7 17.6 8.6 10.8 786.3

Page 11 of 13

### CEMS Data

01/16/2009 12:09 38.56 17.4 8.6 10.8 787.6 01/16/2009 12:10 38.46 17.3 8.6 10.8 788.8 01/16/2009 12:11 38.68 17.9 8.6 10.8 795.1 38.89 17.09 8.60 10.72 790.09 47405194

Date Time SO21 NOX1 CO21 OXY1 FLO1 01/16/2009 12:20 38.32 18.1 8.6 10.8 795.3 01/16/2009 12:21 38.36 18.3 8.6 10.8 791.4 01/16/2009 12:22 38.33 18.2 8.6 10.8 785.3 01/16/2009 12:23 38.15 18.1 8.6 10.8 780.9 01/16/2009 12:24 38.24 18.1 8.6 10.8 778.8 01/16/2009 12:25 38.28 18.4 8.6 10.8 778.1 01/16/2009 12:26 34.78 14.2 5 10.8 783.1 01/16/2009 12:27 3.88 0 0.1 10.8 791.3 01/16/2009 12:28 14.98 10.4 6.7 10.8 795.9 01/16/2009 12:29 36.32 18 8.5 10.8 793.3 01/16/2009 12:30 37.74 18 8.5 10.8 793.7 01/16/2009 12:31 37.8 17.5 8.5 10.8 796.2 01/16/2009 12:32 37.59 17.9 8.5 10.8 791.6 01/16/2009 12:33 37.68 18.4 8.5 10.8 786.1 01/16/2009 12:34 37.63 18.6 8.5 10.8 779.8 01/16/2009 12:35 38.06 18.6 8.5 10.8 789.4 01/16/2009 12:36 37.81 18.3 8.5 10.8 796.1 01/16/2009 12:37 38.2 18.5 8.5 10.8 797.2 01/16/2009 12:38 37.98 18.7 8.5 10.8 788.3 01/16/2009 12:39 37.86 18.8 8.5 10.8 792.5 01/16/2009 12:40 37.82 18.6 8.5 10.8 793.9 01/16/2009 12:41 37.99 18.3 8.5 10.8 791.8 01/16/2009 12:42 37.97 18.5 8.5 10.8 780 01/16/2009 12:43 37.73 18.6 8.5 10.8 781.5 01/16/2009 12:44 37.81 18.7 8.5 10.8 778.9 01/16/2009 12:45 37.61 18.5 8.5 10.8 777 01/16/2009 12:46 37.47 18.6 8.5 10.8 777.7 01/16/2009 12:47 37.49 18.8 8.5 10.8 785.4 01/16/2009 12:48 37.54 18.7 8.5 10.8 790.4 01/16/2009 12:49 37.7 18.3 8.5 10.8 789.3 01/16/2009 12:50 37.76 18.5 8.5 10.8 786.9 01/16/2009 12:51 37.82 18.6 8.6 10.8 800.9 Run 7

Page 12 of 13

### CEMS Data

01/16/2009 12:52 37.62 18.5 8.6 10.8 794.6 01/16/2009 12:53 37.79 18.8 8.6 10.8 779.8 01/16/2009 12:54 37.61 18.7 8.6 10.8 788.1 01/16/2009 12:55 37.83 18.4 8.6 10.8 788.1 01/16/2009 12:56 37.62 18.4 8.6 10.8 798.8 01/16/2009 12:57 37.77 18.5 8.5 10.8 790 01/16/2009 12:58 37.82 18.9 8.6 10.8 788.7 01/16/2009 12:59 37.89 18.4 8.5 10.8 788 01/16/2009 13:00 38.26 18 8.5 10.8 789.4 01/16/2009 13:01 37.7 17.7 8.5 10.8 788.2 01/16/2009 13:02 37.68 18.1 8.5 10.8 789.9 01/16/2009 13:03 37.51 18.5 8.5 10.8 790.7 01/16/2009 13:04 37.82 18.8 8.5 10.8 790.5 01/16/2009 13:05 38.07 18.3 8.5 10.8 792.1 01/16/2009 13:06 37.86 18.3 8.5 10.8 795.7 01/16/2009 13:07 37.86 18.6 8.5 10.8 782.8 01/16/2009 13:08 37.9 18.6 8.5 10.8 788.3 01/16/2009 13:09 37.89 18.5 8.5 10.8 793.3 01/16/2009 13:10 37.78 18.7 8.5 10.8 797.5 01/16/2009 13:11 37.6 18.6 8.5 10.8 792.8 01/16/2009 13:12 37.74 18.5 8.5 10.8 789.6 01/16/2009 13:13 37.8 18.4 8.5 10.8 792.3 01/16/2009 13:14 37.6 18.6 8.5 10.9 791.2 01/16/2009 13:15 37.59 18.8 8.5 10.8 787.2 01/16/2009 13:16 37.48 18.8 8.5 10.8 787.5 01/16/2009 13:17 37.69 18.7 8.5 10.8 794 01/16/2009 13:18 37.83 18.5 8.5 10.8 788.1 01/16/2009 13:19 37.75 18.3 8.5 10.8 790.7 01/16/2009 13:20 37.78 18.1 8.5 10.8 787.7 01/16/2009 13:21 37.65 18.1 8.5 10.8 783.9 01/16/2009 13:22 37.8 18.3 8.5 10.8 795 01/16/2009 13:23 37.96 18.5 8.5 10.8 797.8 01/16/2009 13:24 37.97 18.2 8.5 10.8 793.9 01/16/2009 13:25 37.96 18.5 8.5 10.8 786 01/16/2009 13:26 38.04 18.9 8.5 10.8 784.5 36.913731 17.97 8.315 10.8 789.174627 790.11 47350477.6

Page 13 of 13

## APPENDIX F

TEST PARTICIPANTS

## TEST PARTICIPANTS

AIR SERVICES GROUP TEST TEAM Jorge Varino Environmental Technician – Team Lead Gary Barber Environmental Technician Scott Given Environmental Technician Ryan Newell Associate Technician Raymond A. McDarby Senior Environmental Technician PROCESS DATA Raymond A. McDarby Senior Environmental Technician FUEL ANALYSIS John McDaniel Senior Engineer ing Fellow– Polk Power Station REPORT PREPARATION Raymond A. McDarby Senior Environmental Technician QUALITY ASSURANCE / QUALITY CONTROL Raymond A. McDarby Senior Environmental Technician TEST COORDINATION David A. Smith, QSTI Coordinator, Air Services Group POLK POWER STATION

Michael Perkins Environmental Coordinator Joshua Ellwein Principal Engineer