EMISSIONS TEST REPORT 

BIG BEND STATION 

FACILITY ID NUMBER: 0570039 

EMISSION UNIT ID NO: -002 

UNIT 2 

PARTICULATE MATTER, SULFUR DIOXIDE, and 

VISIBLE EMISSIONS 

April 2, 2008 

Prepared For: 

Tampa Electric Company 

Big Bend Station 

P.O. Box 111 

Tampa, Florida 33601-0111 

Prepared By: 

Tampa Electric Company 

Environmental, Health & Safety 

Environmental Services 

Air Services Group 

Environmental Services 

Air Services Group 

5010 Causeway Boulevard 

Tampa, Florida 33619- 6130 
REPORT CERTIFICATION 

 The sampling and subsequent data entry/reduction detailed in this report 

was conducted at my direction, and I hereby 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 performance, associated quality assurance 

activities, the resultant calculations, and the contents of this report, and certify 

that all project quality objectives have been met. This 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 authentic and accurate to the best of 

my knowledge. 

Signature:__________________________ 

David A. Smith 

Coordinator – Air Services Group 

Environmental Health & Safety 

Tampa Electric Company 
TABLE OF CONTENTS

SECTION PAGE NO.

1.0 SUMMARY OF RESULTS 1 

2.0 DISCUSSION OF RESULTS 2 

3.0 SOURCE DESCRIPTION / TEST PROCEDURES 3 

4.0 TABULATED RESULTS 

SOOT BLOWING PARTICULATE TEST SUMMARY 6 

NON SOOT BLOWING PARTICULATE TEST SUMMARY 7 

SULFUR DIOXIDE INFORMATION SUMMARY 8 

SOOT BLOWING OPACITY DATA SUMMARY 9 

NON SOOT BLOWING OPACITY DATA SUMMARY 10 

HEAT INPUT CALCULATIONS 11 

 4.0 FIGURES 

FIGURE 1 SAMPLING LOCATION DIAGRAM 13 

APPENDICES

A. PARTICULATE MATTER CALCULATIONS

B. PARTICULATE MATTER LABORATORY ANALYTICAL DATA

C. BOILER/PRECIPITATOR OPERATIONAL DATA

D. PLANT CEMS DAHS PRINTOUTS

E. FUEL ANALYSIS

F. FIELD DATA SHEETS

G. SAMPLING EQUIPMENT CALIBRATIONS

H. CHAIN OF CUSTODY

I. TEST PARTICIPANTS
1.0 INTRODUCTION

On April 2, 2008, Tampa Electric Company’s Environmental, Health, & Safety Air 

Services Group, performed source emission tests at the Big Bend Station Boiler 

No. 2, emissions unit I.D. # -002. Testing was conducted in accordance with the 

Title V Permit #0570039-028-AV, Conditions A.12 through A.14. 

1 
2.0 DISCUSSION OF RESULTS

The particulate matter emission rate under both soot blowing, and non-soot 

blowing conditions were derived from three United States Environmental 

Protection Agency (USEPA) Reference Method 5B test runs. Under soot blowing 

conditions the average of the three test runs was 0.03 lb/mmBtu. Under nonsoot blowing conditions the average of the three test runs was 0.03 lb/mmBtu. 

The USEPA Consent Decree allowable emission rate under either condition is 

0.03 lb/mmBtu. 

The Sulfur Dioxide (SO2) emission rate was determined using data provided by 

the Continuous Emissions Monitoring System’s (CEMS) Data Acquisition and 

Handling System (DAHS). The average emission rate for the test period was 

determined to be 0.1 lb/mmBtu, and 298 lbs/hr. The FDEP allowable emission 

rate is 6.5 lbs/mmBtu based on a two hour average, and 3277 lbs/hr based on 

scenario 3 as listed in condition A.9 of the permit. 

Visible emissions were evaluated using a United Sciences Incorporated, Model 

500C transmissometer (S/N 5001689), during both soot blowing and non-soot 

blowing testing. The 1-hour average opacity under soot blowing conditions was 

9%. The 1-hour average opacity under non-soot blowing conditions was 8%. 

The FDEP allowable emission rate is 20 percent opacity. 

During the test performed on April 2, 2008, Boiler No. 2 was operated at an 

average heat input rate of 3929 mmBtu/hr. The average quantity of fuel burned 

was 166.4 tons per hour. Based on the permitted maximum heat input rate of 

3996 mmBtu/hr, the capacity factor for this test was determined to be 98%. 

2 
3.0 SOURCE DESCRIPTION/TEST PROCEDURES

Big Bend Station is located on Big Bend Road, Ruskin, Florida at UTM 

coordinates East 361.9 North 3075.0. The Boiler No. 2 particulate matter 

sampling location consists of a shared circular stack 29.83 feet in diameter with 

four sample ports located 90 degrees apart on the stack circumference. These 

ports are located downstream of the electrostatic precipitator and the FGD 

scrubber. The sampling ports were determined to be 8.74 diameters 

downstream of the transition ductwork and 2.42 diameters upstream of the stack 

exit. Using these criteria, a total of 12 sampling points were chosen for 

particulate sampling as stipulated in the USEPA Method 1 test procedure. During 

this test, Boiler No. 1 was not operating, and was isolated from the FGD module. 

A diagram of the stack sampling location is included in Figure 1 along with other 

pertinent information on the test site. 

Boiler No. 2 is serviced by an electrostatic precipitator for the control of flyash 

emissions, and a flue gas desulfurization (FGD) system for control of sulfur 

dioxide emissions. Generator and precipitator operations data is included in 

Appendix C of this report. 

Particulate sampling was performed according to USEPA Method 5B 

"Determination of Nonsulfuric Acid Particulate Matter from Stationary Sources". 

Individual test run calculations are included as Appendix A of this report. 

Particulate matter laboratory analysis may be found in Appendix B of this report. 

Diluent gas sampling and analysis was performed according to USEPA Method 

3B "Gas Analysis for Determination of Emission Rate Correction Factor or 

Excess Air”. Gas analysis was performed on-site using an Orsat analyzer. 

Sulfur Dioxide (SO2) and Carbon Dioxide (CO2) data were provided by the 

Continuous Emissions Monitoring System (CEMS) Data Acquisition and Handling 

3 
System (DAHS). Averages were derived from the time frame of 7:40 through 

16:22 on April 2, 2008. This data is included as Appendix D of this report. 

Visible emissions were assessed using the installed Continuous Opacity Monitor 

(COM), and the CEMS DAHS. 

4 
4.0 TABULATED RESULTS

5 
BIG BEND STATION

PARTICULATE MATTER DATA SUMMARY

Run 1s Run 2s Run 3s

Vm(std), scf 37.542 36.185 35.040

Bws, ratio 0.151 0.151 0.151

O2, % volume 9.00 9.00 9.00

Md, lb/lb - mole 29.96 29.96 29.96

Ms, lb/lb - mole 28.16 28.16 28.16

Qs, acf/min 1331539.3 1292618.4 1243964.2

Qs(std), dscf/min 1009297.4 977836.2 940788.7

I, % 102.6 102.1 102.8

C, lbs/dscf 1.894E-06 1.590E-06 1.762E-06

Er, lb/mmBtu 0.03 0.03 0.03

Emission rate (Er), lb/mmBtu, calculated as: C x 9780 dscf/mmBtu x (20.9/(20.9-%O2))

102.50

1.7485E-06

0.03

29.960

28.160

1289373.96

975974.12

Test Summary

36.256

0.1505

9.00

Boiler #2

WET-BOTTOM UTILITY BOILER

April 2, 2008

SOOT BLOWING

6 
BIG BEND STATION

PARTICULATE MATTER DATA SUMMARY

Run 1 Run 2 Run 3

Vm(std), scf 37.772 36.577 34.856

Bws, ratio 0.146 0.148 0.140

O2, % volume 9.00 9.00 9.00

Md, lb/lb - mole 29.96 29.96 29.96

Ms, lb/lb - mole 28.21 28.19 28.29

Qs, acf/min 1340362.9 1304689.2 1238294.7

Qs(std), dscf/min 1024958.5 991479.7 949244.0

I, % 101.7 101.8 101.3

C, lbs/dscf 1.605E-06 1.775E-06 2.046E-06

Er, lb/mmBtu 0.03 0.03 0.04

Emission rate (Er), lb/mmBtu, calculated as: C x 9780 dscf/mmBtu x (20.9/(20.9-%O2))

1.8087E-06

0.03

NON - SOOT BLOWING

28.229

1294448.95

988560.74

101.60

36.402

0.1447

9.00

29.960

Boiler #2

WET-BOTTOM UTILITY BOILER

April 2, 2008

Test Summary

7 
BIG BEND STATION

SULFUR DIOXIDE DATA FROM CEMs

Test Period Information

Start Time 7:40:00 Eastern Standard Time (EST)

Stop Time 16:22:00 Eastern Standard Time (EST)

Total Time 8:42:00

Corresponding to the time frame for the PM test.

Sulfur Dioxide Data:

SO2 CO2 SO2 SO2

ppmvw %, wet lb/mmBtu lbs/hr

24.88 9.83 0.1 298

Calculation Details

SO2, lb/mmBtu = SO2, ppmvw x Cf x Fc x (100 / CO2 %, wet)

where:

Cf = 1.6635E-07 (lb/scf)/ppm SO2

Fc = 1800 scf/mmBtu

SO2, lbs/hr = SO2, lb/mmBtu x Heat Input, mmBtu/hr

where:

Heat Input = 3929 mmBtu/hr, from Heat Input Calculation

Unit #2

WET-BOTTOM UTILITY BOILER

April 2, 2008

CEM DATA RM - 19

8 
Facility: Big Bend Station

Unit: Unit 2

Operating Conditions: Sootblowing

Record# DATE TIME OPA62 Record# DATE TIME OPA62

1 4/2/08 9:07 9.4 31 4/2/08 9:37 9.1

2 4/2/08 9:08 9.7 32 4/2/08 9:38 8.6

3 4/2/08 9:09 9.8 33 4/2/08 9:39 8.4

4 4/2/08 9:10 9.8 34 4/2/08 9:40 8.4

5 4/2/08 9:11 9.8 35 4/2/08 9:41 8.4

6 4/2/08 9:12 9.8 36 4/2/08 9:42 8.4

7 4/2/08 9:13 9.8 37 4/2/08 9:43 8.4

8 4/2/08 9:14 9.4 38 4/2/08 9:44 8.7

9 4/2/08 9:15 9.2 39 4/2/08 9:45 9.0

10 4/2/08 9:16 9.2 40 4/2/08 9:46 9.0

11 4/2/08 9:17 9.2 41 4/2/08 9:47 9.0

12 4/2/08 9:18 9.2 42 4/2/08 9:48 9.0

13 4/2/08 9:19 9.2 43 4/2/08 9:49 9.0

14 4/2/08 9:20 9.2 44 4/2/08 9:50 8.8

15 4/2/08 9:21 9.3 45 4/2/08 9:51 8.5

16 4/2/08 9:22 9.4 46 4/2/08 9:52 8.5

17 4/2/08 9:23 9.4 47 4/2/08 9:53 8.5

18 4/2/08 9:24 9.4 48 4/2/08 9:54 8.5

19 4/2/08 9:25 9.4 49 4/2/08 9:55 8.5

20 4/2/08 9:26 9.3 50 4/2/08 9:56 8.8

21 4/2/08 9:27 9.3 51 4/2/08 9:57 9.0

22 4/2/08 9:28 9.3 52 4/2/08 9:58 9.0

23 4/2/08 9:29 9.3 53 4/2/08 9:59 9.0

24 4/2/08 9:30 9.3 54 4/2/08 10:00 9.0

25 4/2/08 9:31 9.3 55 4/2/08 10:01 9.0

26 4/2/08 9:32 9.2 56 4/2/08 10:02 9.2

27 4/2/08 9:33 9.1 57 4/2/08 10:03 9.5

28 4/2/08 9:34 9.1 58 4/2/08 10:04 9.5

29 4/2/08 9:35 9.1 59 4/2/08 10:05 9.5

30 4/2/08 9:36 9.1 60 4/2/08 10:06 9.5

Test Average: 9.12 %

Minimum One Minute Average: 8.40 %

Maximum One Minute Average: 9.80 %

Maximum Six Minute Average: 9.78 %

Visible Emissions Determination from Opacity Monitor

9 
Facility: Big Bend Station

Unit: Unit 2

Operating Conditions: Non-sootblowing

Record# DATE TIME OPA62 Record# DATE TIME OPA62

1 4/2/08 10:53 8.5 31 4/2/08 11:23 8.0

2 4/2/08 10:54 8.5 32 4/2/08 11:24 8.0

3 4/2/08 10:55 8.5 33 4/2/08 11:25 8.0

4 4/2/08 10:56 8.4 34 4/2/08 11:26 8.1

5 4/2/08 10:57 8.4 35 4/2/08 11:27 8.3

6 4/2/08 10:58 8.4 36 4/2/08 11:28 8.3

7 4/2/08 10:59 8.4 37 4/2/08 11:29 8.3

8 4/2/08 11:00 8.4 38 4/2/08 11:30 8.3

9 4/2/08 11:01 8.4 39 4/2/08 11:31 8.3

10 4/2/08 11:02 8.3 40 4/2/08 11:32 8.2

11 4/2/08 11:03 8.3 41 4/2/08 11:33 8.0

12 4/2/08 11:04 8.3 42 4/2/08 11:34 8.0

13 4/2/08 11:05 8.3 43 4/2/08 11:35 8.0

14 4/2/08 11:06 8.3 44 4/2/08 11:36 8.0

15 4/2/08 11:07 8.3 45 4/2/08 11:37 8.0

16 4/2/08 11:08 8.6 46 4/2/08 11:38 8.1

17 4/2/08 11:09 8.8 47 4/2/08 11:39 8.2

18 4/2/08 11:10 8.8 48 4/2/08 11:40 8.2

19 4/2/08 11:11 8.8 49 4/2/08 11:41 8.2

20 4/2/08 11:12 8.8 50 4/2/08 11:42 8.2

21 4/2/08 11:13 8.8 51 4/2/08 11:43 8.2

22 4/2/08 11:14 8.3 52 4/2/08 11:44 8.0

23 4/2/08 11:15 7.8 53 4/2/08 11:45 7.8

24 4/2/08 11:16 7.8 54 4/2/08 11:46 7.8

25 4/2/08 11:17 7.8 55 4/2/08 11:47 7.8

26 4/2/08 11:18 7.8 56 4/2/08 11:48 7.8

27 4/2/08 11:19 7.8 57 4/2/08 11:49 7.8

28 4/2/08 11:20 7.9 58 4/2/08 11:50 7.9

29 4/2/08 11:21 8.0 59 4/2/08 11:51 7.9

30 4/2/08 11:22 8.0 60 4/2/08 11:52 7.9

Test Average: 8.18 %

Minimum One Minute Average: 7.80 %

Maximum One Minute Average: 8.80 %

Maximum Six Minute Average: 8.77 %

Visible Emissions Determination from Opacity Monitor

10 
BIG BEND GENERATING STATION

HEAT INPUT CALCULATIONS

Gross Heat Rate, Previous Month (March): 10353 KMBtu/MWh

1.0353E+07 MMBtu/MWh

MegaWatt Hour Integrator Information

Initial Integrator Reading: 898026 MWh

Final Integrator Reading: 901358 MWh

Total: 3332 MWh

Test Time Information

Testing Start Time: 7:40

Testing End Time: 16:27

Total Test Time: 8.78 hours

Calculated Heat Input

Average Unit Load, MW = MWh / hours: 379.5 MW

Heat Input, MMBtu/h = MMBtu/MWh x MW: 3929 mmBtu/hr

Fuel Consumption Calculation

Laboratory Sample ID: AA93807

Btu as received: 11803 Btu/lb

Tons of Fuel Consumed, Tons/hr = (mmBtu/h / Btu/lb) x 500: 166.4 Tons/hour

Unit #2

April 2, 2008

WET-BOTTOM UTILTIY BOILER

11 
5.0 FIGURES

12 
FIGURE 1

EXHAUST STACK

426.5 ’ EL.

BIG BEND GENERATING STATION

PARTICULATE TRAVERSE POINTS

OUTLET

N

PORT LOCATION PLAN

REVISED: 10-Jan-06

CS0W1 (BOILERS 1 & 2) TEST LOCATION

STACK DIAMETERS DOWNSTREAM

FROM DISTURBANCE = 8.74

STACK DIAMETERS UPSTREAM

FROM DISTURBANCE = 2.42

STACK DIAMETER = 29.917 FT. ID.

STACK AREA = 702.952 SQ. FT.

PORT LENGTH = 62 IN.

TRAVERSE

POINT 

1

2

3

% OF

STACK DIAMETER

IN. FROM

STACK WALL

4.4%

14.6%

29.6%

15.80 IN.

52.41 IN.

106.27 IN.

.

499 ’ EL.

165 ’ EL.

261.5 ’

FGD

PRESSURIZED

ANNULUS

72.5 ’

A

B C

D

9 ’ EL.

13 
APPENDIX A

PARTICULATE MATTER CALCULATIONS 
Environmental, Health, & Safety

Air Services Group

40 CFR 60, Appendix A - Test Methods

Reference Method 5/17

Particulate Test Calculations

Customer: Tampa Electric Company

Facility: Big Bend Station

Sampling Location: CS0W1 - Common Stack 1 - Wet

Unit Under Test: Boiler #2

Operating Conditions: Soot Blowing

Run Number: 1s

Date: April 2, 2008

Sample Time, θ: 60 minutes Nozzle Diameter, Dn: 0.279 inches

Barometric Pressure, Pb: 29.72 "Hg Nozzle Area, An: 0.000425 ft2

Stack Pressure, Ps: 29.71 "Hg Average Orifice Meter, ΔH: 1.334 "H2O

Effective Stack Area, As: 702.952 ft2 Sample Volume, Vm: 39.563 ft3

Pitot Coefficient, Cp: 0.84 dimensionless Average Meter Temp., Tm: 93.4 o

F

Gas Analysis: 10.0 % CO2 Average Stack Temp., Ts: 127.6 o

F

9.0 % O2 Average √Δp: 0.525 "H2O

0.0 % CO Condensate Volume, Vlc: 141.1 ml

81.0 % N2 Meter Box Y: 0.998 dimensionless

F-factor, Fd, for fuel: 9780 dscf/MMBtu

Data Calculated from Source Measurements:

Vw(std) = 4.714E-02 x Vlc 6.651 scf

Vm(std) = 17.647 x Vm x Y x (Pb + (ΔH / 13.6)) / (Tm +460) 37.542 dscf

Bws = Vw(std) / (Vm(std) + Vw(std)) 0.151 %

FDA = 1.0 - Bws 0.849 %

Md = (0.44 x %CO2) + (0.32 x %O2) + (0.28 x (%N2 + % CO)) 29.96 lb./lb. mole

Ms = (Md x FDA) + (18.0 x Bws) 28.16 lb./lb. mole

vs = 85.49 x Cp x (√Δp) x (√(Ts + 460) / (Ms x Ps)) 31.57 ft/second

Qs = vs x As x 60 1331539.3 acf/minute

Qs(std) = Qs x FDA x (528 / (Ts + 460)) x (Ps / 29.92)) 1009297.4 dscf/minute

I = (Ts + 460) x ((2.67E-03 x Vlc) + (Vm(std) / 17.647)) x 100 / (θ x Ps x An x vs x 60) 102.6 %

Data from Laboratory Analysis:

Total Particulate Weight From Laboratory Analysis: 0.03225 grams

Calculated Concentration and Emission Rate Data:

cs = (15.432 x grams) / Vm(std) 0.013 grains/dscf

grains/acf = cs x 17.647 x Ps x (FDA / (Ts + 460) 0.010 grains/acf

C = cs / 7000 1.894E-06 lbs/dscf

ER = C x Fd x (20.9 /(20.9 - %O2) 0.033 lbs/MMBtu
Environmental, Health, & Safety

Air Services Group

40 CFR 60, Appendix A - Test Methods

Reference Method 5/17

Particulate Test Calculations

Customer: Tampa Electric Company

Facility: Big Bend Station

Sampling Location: CS0W1 - Common Stack 1 - Wet

Unit Under Test: Boiler #2

Operating Conditions: Soot Blowing

Run Number: 2s

Date: April 2, 2008

Sample Time, θ: 60 minutes Nozzle Diameter, Dn: 0.279 inches

Barometric Pressure, Pb: 29.75 "Hg Nozzle Area, An: 0.000425 ft2

Stack Pressure, Ps: 29.74 "Hg Average Orifice Meter, ΔH: 1.273 "H2O

Effective Stack Area, As: 702.952 ft2 Sample Volume, Vm: 38.794 ft3

Pitot Coefficient, Cp: 0.84 dimensionless Average Meter Temp., Tm: 103.5 o

F

Gas Analysis: 10.0 % CO2 Average Stack Temp., Ts: 129.3 o

F

9.0 % O2 Average √Δp: 0.509 "H2O

0.0 % CO Condensate Volume, Vlc: 136.0 ml

81.0 % N2 Meter Box Y: 0.998 dimensionless

F-factor, Fd, for fuel: 9780 dscf/MMBtu

Data Calculated from Source Measurements:

Vw(std) = 4.714E-02 x Vlc 6.411 scf

Vm(std) = 17.647 x Vm x Y x (Pb + (ΔH / 13.6)) / (Tm +460) 36.185 dscf

Bws = Vw(std) / (Vm(std) + Vw(std)) 0.151 %

FDA = 1.0 - Bws 0.849 %

Md = (0.44 x %CO2) + (0.32 x %O2) + (0.28 x (%N2 + % CO)) 29.96 lb./lb. mole

Ms = (Md x FDA) + (18.0 x Bws) 28.16 lb./lb. mole

vs = 85.49 x Cp x (√Δp) x (√(Ts + 460) / (Ms x Ps)) 30.65 ft/second

Qs = vs x As x 60 1292618.4 acf/minute

Qs(std) = Qs x FDA x (528 / (Ts + 460)) x (Ps / 29.92)) 977836.2 dscf/minute

I = (Ts + 460) x ((2.67E-03 x Vlc) + (Vm(std) / 17.647)) x 100 / (θ x Ps x An x vs x 60) 102.1 %

Data from Laboratory Analysis:

Total Particulate Weight From Laboratory Analysis: 0.02610 grams

Calculated Concentration and Emission Rate Data:

cs = (15.432 x grams) / Vm(std) 0.011 grains/dscf

grains/acf = cs x 17.647 x Ps x (FDA / (Ts + 460) 0.008 grains/acf

C = cs / 7000 1.590E-06 lbs/dscf

ER = C x Fd x (20.9 /(20.9 - %O2) 0.027 lbs/MMBtu
Environmental, Health, & Safety

Air Services Group

40 CFR 60, Appendix A - Test Methods

Reference Method 5/17

Particulate Test Calculations

Customer: Tampa Electric Company

Facility: Big Bend Station

Sampling Location: CS0W1 - Common Stack 1 - Wet

Unit Under Test: Boiler #2

Operating Conditions: Soot Blowing

Run Number: 3s

Date: April 2, 2008

Sample Time, θ: 60 minutes Nozzle Diameter, Dn: 0.279 inches

Barometric Pressure, Pb: 29.75 "Hg Nozzle Area, An: 0.000425 ft2

Stack Pressure, Ps: 29.74 "Hg Average Orifice Meter, ΔH: 1.196 "H2O

Effective Stack Area, As: 702.952 ft2 Sample Volume, Vm: 38.144 ft3

Pitot Coefficient, Cp: 0.84 dimensionless Average Meter Temp., Tm: 111.8 o

F

Gas Analysis: 10.0 % CO2 Average Stack Temp., Ts: 129.4 o

F

9.0 % O2 Average √Δp: 0.490 "H2O

0.0 % CO Condensate Volume, Vlc: 131.8 ml

81.0 % N2 Meter Box Y: 0.998 dimensionless

F-factor, Fd, for fuel: 9780 dscf/MMBtu

Data Calculated from Source Measurements:

Vw(std) = 4.714E-02 x Vlc 6.213 scf

Vm(std) = 17.647 x Vm x Y x (Pb + (ΔH / 13.6)) / (Tm +460) 35.040 dscf

Bws = Vw(std) / (Vm(std) + Vw(std)) 0.151 %

FDA = 1.0 - Bws 0.849 %

Md = (0.44 x %CO2) + (0.32 x %O2) + (0.28 x (%N2 + % CO)) 29.96 lb./lb. mole

Ms = (Md x FDA) + (18.0 x Bws) 28.16 lb./lb. mole

vs = 85.49 x Cp x (√Δp) x (√(Ts + 460) / (Ms x Ps)) 29.49 ft/second

Qs = vs x As x 60 1243964.2 acf/minute

Qs(std) = Qs x FDA x (528 / (Ts + 460)) x (Ps / 29.92)) 940788.7 dscf/minute

I = (Ts + 460) x ((2.67E-03 x Vlc) + (Vm(std) / 17.647)) x 100 / (θ x Ps x An x vs x 60) 102.8 %

Data from Laboratory Analysis:

Total Particulate Weight From Laboratory Analysis: 0.02800 grams

Calculated Concentration and Emission Rate Data:

cs = (15.432 x grams) / Vm(std) 0.012 grains/dscf

grains/acf = cs x 17.647 x Ps x (FDA / (Ts + 460) 0.009 grains/acf

C = cs / 7000 1.762E-06 lbs/dscf

ER = C x Fd x (20.9 /(20.9 - %O2) 0.030 lbs/MMBtu
Environmental, Health, & Safety

Air Services Group

40 CFR 60, Appendix A - Test Methods

Reference Method 5/17

Particulate Test Calculations

Customer: Tampa Electric Company

Facility: Big Bend Station

Sampling Location: CS0W1 - Common Stack 1 - Wet

Unit Under Test: Boiler #2

Operating Conditions: Non-Soot Blowing

Run Number: 1

Date: April 2, 2008

Sample Time, θ: 60 minutes Nozzle Diameter, Dn: 0.279 inches

Barometric Pressure, Pb: 29.72 "Hg Nozzle Area, An: 0.000425 ft2

Stack Pressure, Ps: 29.71 "Hg Average Orifice Meter, ΔH: 1.349 "H2O

Effective Stack Area, As: 702.952 ft2 Sample Volume, Vm: 39.390 ft3

Pitot Coefficient, Cp: 0.84 dimensionless Average Meter Temp., Tm: 87.7 o

F

Gas Analysis: 10.0 % CO2 Average Stack Temp., Ts: 125.5 o

F

9.0 % O2 Average √Δp: 0.529 "H2O

0.0 % CO Condensate Volume, Vlc: 137.0 ml

81.0 % N2 Meter Box Y: 0.998 dimensionless

F-factor, Fd, for fuel: 9780 dscf/MMBtu

Data Calculated from Source Measurements:

Vw(std) = 4.714E-02 x Vlc 6.458 scf

Vm(std) = 17.647 x Vm x Y x (Pb + (ΔH / 13.6)) / (Tm +460) 37.772 dscf

Bws = Vw(std) / (Vm(std) + Vw(std)) 0.146 %

FDA = 1.0 - Bws 0.854 %

Md = (0.44 x %CO2) + (0.32 x %O2) + (0.28 x (%N2 + % CO)) 29.96 lb./lb. mole

Ms = (Md x FDA) + (18.0 x Bws) 28.21 lb./lb. mole

vs = 85.49 x Cp x (√Δp) x (√(Ts + 460) / (Ms x Ps)) 31.78 ft/second

Qs = vs x As x 60 1340362.9 acf/minute

Qs(std) = Qs x FDA x (528 / (Ts + 460)) x (Ps / 29.92)) 1024958.5 dscf/minute

I = (Ts + 460) x ((2.67E-03 x Vlc) + (Vm(std) / 17.647)) x 100 / (θ x Ps x An x vs x 60) 101.7 %

Data from Laboratory Analysis:

Total Particulate Weight From Laboratory Analysis: 0.02750 grams

Calculated Concentration and Emission Rate Data:

cs = (15.432 x grams) / Vm(std) 0.011 grains/dscf

grains/acf = cs x 17.647 x Ps x (FDA / (Ts + 460) 0.009 grains/acf

C = cs / 7000 1.605E-06 lbs/dscf

ER = C x Fd x (20.9 /(20.9 - %O2) 0.028 lbs/MMBtu
Environmental, Health, & Safety

Air Services Group

40 CFR 60, Appendix A - Test Methods

Reference Method 5/17

Particulate Test Calculations

Customer: Tampa Electric Company

Facility: Big Bend Station

Sampling Location: CS0W1 - Common Stack 1 - Wet

Unit Under Test: Boiler #2

Operating Conditions: Non-Soot Blowing

Run Number: 2

Date: April 2, 2008

Sample Time, θ: 60 minutes Nozzle Diameter, Dn: 0.279 inches

Barometric Pressure, Pb: 29.75 "Hg Nozzle Area, An: 0.000425 ft2

Stack Pressure, Ps: 29.74 "Hg Average Orifice Meter, ΔH: 1.295 "H2O

Effective Stack Area, As: 702.952 ft2 Sample Volume, Vm: 38.952 ft3

Pitot Coefficient, Cp: 0.84 dimensionless Average Meter Temp., Tm: 99.8 o

F

Gas Analysis: 10.0 % CO2 Average Stack Temp., Ts: 128.3 o

F

9.0 % O2 Average √Δp: 0.514 "H2O

0.0 % CO Condensate Volume, Vlc: 135.0 ml

81.0 % N2 Meter Box Y: 0.998 dimensionless

F-factor, Fd, for fuel: 9780 dscf/MMBtu

Data Calculated from Source Measurements:

Vw(std) = 4.714E-02 x Vlc 6.364 scf

Vm(std) = 17.647 x Vm x Y x (Pb + (ΔH / 13.6)) / (Tm +460) 36.577 dscf

Bws = Vw(std) / (Vm(std) + Vw(std)) 0.148 %

FDA = 1.0 - Bws 0.852 %

Md = (0.44 x %CO2) + (0.32 x %O2) + (0.28 x (%N2 + % CO)) 29.96 lb./lb. mole

Ms = (Md x FDA) + (18.0 x Bws) 28.19 lb./lb. mole

vs = 85.49 x Cp x (√Δp) x (√(Ts + 460) / (Ms x Ps)) 30.93 ft/second

Qs = vs x As x 60 1304689.2 acf/minute

Qs(std) = Qs x FDA x (528 / (Ts + 460)) x (Ps / 29.92)) 991479.7 dscf/minute

I = (Ts + 460) x ((2.67E-03 x Vlc) + (Vm(std) / 17.647)) x 100 / (θ x Ps x An x vs x 60) 101.8 %

Data from Laboratory Analysis:

Total Particulate Weight From Laboratory Analysis: 0.02945 grams

Calculated Concentration and Emission Rate Data:

cs = (15.432 x grams) / Vm(std) 0.012 grains/dscf

grains/acf = cs x 17.647 x Ps x (FDA / (Ts + 460) 0.009 grains/acf

C = cs / 7000 1.775E-06 lbs/dscf

ER = C x Fd x (20.9 /(20.9 - %O2) 0.030 lbs/MMBtu
Environmental, Health, & Safety

Air Services Group

40 CFR 60, Appendix A - Test Methods

Reference Method 5/17

Particulate Test Calculations

Customer: Tampa Electric Company

Facility: Big Bend Station

Sampling Location: CS0W1 - Common Stack 1 - Wet

Unit Under Test: Boiler #2

Operating Conditions: Non-Soot Blowing

Run Number: 3

Date: April 2, 2008

Sample Time, θ: 60 minutes Nozzle Diameter, Dn: 0.279 inches

Barometric Pressure, Pb: 29.75 "Hg Nozzle Area, An: 0.000425 ft2

Stack Pressure, Ps: 29.74 "Hg Average Orifice Meter, ΔH: 1.185 "H2O

Effective Stack Area, As: 702.952 ft2 Sample Volume, Vm: 37.693 ft3

Pitot Coefficient, Cp: 0.84 dimensionless Average Meter Temp., Tm: 108.3 o

F

Gas Analysis: 10.0 % CO2 Average Stack Temp., Ts: 128.8 o

F

9.0 % O2 Average √Δp: 0.489 "H2O

0.0 % CO Condensate Volume, Vlc: 120.4 ml

81.0 % N2 Meter Box Y: 0.998 dimensionless

F-factor, Fd, for fuel: 9780 dscf/MMBtu

Data Calculated from Source Measurements:

Vw(std) = 4.714E-02 x Vlc 5.676 scf

Vm(std) = 17.647 x Vm x Y x (Pb + (ΔH / 13.6)) / (Tm +460) 34.856 dscf

Bws = Vw(std) / (Vm(std) + Vw(std)) 0.140 %

FDA = 1.0 - Bws 0.860 %

Md = (0.44 x %CO2) + (0.32 x %O2) + (0.28 x (%N2 + % CO)) 29.96 lb./lb. mole

Ms = (Md x FDA) + (18.0 x Bws) 28.29 lb./lb. mole

vs = 85.49 x Cp x (√Δp) x (√(Ts + 460) / (Ms x Ps)) 29.36 ft/second

Qs = vs x As x 60 1238294.7 acf/minute

Qs(std) = Qs x FDA x (528 / (Ts + 460)) x (Ps / 29.92)) 949244.0 dscf/minute

I = (Ts + 460) x ((2.67E-03 x Vlc) + (Vm(std) / 17.647)) x 100 / (θ x Ps x An x vs x 60) 101.3 %

Data from Laboratory Analysis:

Total Particulate Weight From Laboratory Analysis: 0.03235 grams

Calculated Concentration and Emission Rate Data:

cs = (15.432 x grams) / Vm(std) 0.0143 grains/dscf

grains/acf = cs x 17.647 x Ps x (FDA / (Ts + 460) 0.0110 grains/acf

C = cs / 7000 2.046E-06 lbs/dscf

ER = C x Fd x (20.9 /(20.9 - %O2) 0.035 lbs/MMBtu
APPENDIX B

PARTICULATE MATTER LABORATORY ANALYTICAL DATA 
Customer AIR SERVICES Plant BIG BEND Unit 2/CS01W

Method 5-B Stack Test Completion Date 04/02/2008Analyst SS Sample Number AA93807

ACETONE BEAKER 1st weighing Date 04/09/2008 Time 11:05 % RH 51.0%

2nd weighing Date 04/10/2008 Time 11:35 % RH 50.0%

3rd weighing Date Time % RH

4th weighing Date Time % RH

***Blank*** Run 1 Run 2 Run 3 Run 1S Run 2S Run 3S

Acetone Container ID AIR IK AIR IC AIR IA AIR IE AIR IF AIR IB AIR ID

Acetone Rinse Vol.(Va), mls 150.0000 150 150 150 150 150 150

1st Gross Wt., grams 97.4541 105.1420 103.9537 106.2446 111.5206 105.8612 101.4112

2nd Gross Wt., grams 97.4540 105.1419 103.9535 106.2449 111.5206 105.8612 101.4113

3rd Gross Wt., grams

4th Gross Wt., grams

Avg. Gross Wt., grams 97.45405 105.14195 103.95360 106.24475 111.52060 105.86120 101.41125

Tare Wt., grams 97.45445 105.13630 103.94875 106.23520 111.51325 105.85775 101.40515

Acetone Blank Wt., mg -0.40 -0.40 -0.40 -0.40 -0.40 -0.40 -0.40

Acetone Particulate Wt., mg 6.05 5.25 9.95 7.75 3.85 6.50

Acetone Residue, mg/g -0.0034

Acetone Blank Criteria OK to subtract acetone blank

 FILTER 1st weighing Date 04/09/2008 Time 11:25 % RH 51.0%

Date 04/10/2008 Time 11:55 % RH 50.0%

3rd weighing Date Time % RH

4th weighing Date Time % RH

Filter/Thimble ID 203073 203079 203078 203.074 203077 203076 203075

1st Gross Wt., grams 0.2527 0.2730 0.2767 0.2744 0.2752 0.2738 0.2746

2nd Gross Wt., grams 0.2527 0.2733 0.2764 0.2743 0.2752 0.2741 0.2743

3rd Gross Wt., grams

4th Gross Wt., grams

Avg. Gross Wt., grams 0.25270 0.27315 0.27655 0.27435 0.27520 0.27395 0.27445

Tare Wt., grams 0.25270 0.25170 0.25235 0.25195 0.25070 0.25170 0.25295

Filter Particulate Wt., mg 21.45 24.20 22.40 24.50 22.25 21.50

Difference, milligrams 0

Total Sample Particulate Wt., mg 27.50 29.45 32.35 32.25 26.10 28.00

0.0275 0.02945 0.03235 0.03225 0.0261 0.028

Start Here
APPENDIX C

BOILER/PRECIPITATOR OPERATIONAL DATA



























APPENDIX D

PLANT CEMS DAHS PRINTOUTS
Big Bend Unit 2 Compliance SO2 Data 

Date Time SO21 CO21

04/02/2008 7:40 20.8 9.6

04/02/2008 7:41 18.8 9.5

04/02/2008 7:42 18.8 9.5

04/02/2008 7:43 19.4 9.5

04/02/2008 7:44 19.7 9.5

04/02/2008 7:45 21.1 9.5

04/02/2008 7:46 20.8 9.4

04/02/2008 7:47 19.9 9.4

04/02/2008 7:48 19.4 9.4

04/02/2008 7:49 20.4 9.5

04/02/2008 7:50 19.9 9.6

04/02/2008 7:51 20.9 9.6

04/02/2008 7:52 19.8 9.4

04/02/2008 7:53 19.9 9.4

04/02/2008 7:54 19.6 9.4

04/02/2008 7:55 20.5 9.4

04/02/2008 7:56 20.7 9.4

04/02/2008 7:57 20.7 9.4

04/02/2008 7:58 20.6 9.4

04/02/2008 7:59 22.1 9.4

04/02/2008 8:00 22.1 9.6

04/02/2008 8:01 22.4 9.7

04/02/2008 8:02 21.3 9.6

04/02/2008 8:03 20.3 9.4

04/02/2008 8:04 19.3 9.3

04/02/2008 8:05 18.8 9.4

04/02/2008 8:06 18.8 9.6

04/02/2008 8:07 18.6 9.6

04/02/2008 8:08 18 9.6

04/02/2008 8:09 18.5 9.5

04/02/2008 8:10 18.1 9.5

04/02/2008 8:11 18.5 9.4

04/02/2008 8:12 18.4 9.4

04/02/2008 8:13 18.9 9.4

04/02/2008 8:14 18.8 9.4

Page 1 of 15
Big Bend Unit 2 Compliance SO2 Data 

Date Time SO21 CO21

04/02/2008 8:15 18.8 9.3

04/02/2008 8:16 19.1 9.4

04/02/2008 8:17

04/02/2008 8:18

04/02/2008 8:19

04/02/2008 8:20

04/02/2008 8:21

04/02/2008 8:22

04/02/2008 8:23

04/02/2008 8:24

04/02/2008 8:25

04/02/2008 8:26

04/02/2008 8:27

04/02/2008 8:28

04/02/2008 8:29

04/02/2008 8:30

04/02/2008 8:31

04/02/2008 8:32

04/02/2008 8:33

04/02/2008 8:34

04/02/2008 8:35

04/02/2008 8:36

04/02/2008 8:37

04/02/2008 8:38

04/02/2008 8:39

04/02/2008 8:40

04/02/2008 8:41

04/02/2008 8:42

04/02/2008 8:43

04/02/2008 8:44

04/02/2008 8:45

04/02/2008 8:46

04/02/2008 8:47

04/02/2008 8:48

04/02/2008 8:49 31.8 4.4

04/02/2008 8:50 38.2 8.7

04/02/2008 8:51 34.9 9.2

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Calibration in Progress

Page 2 of 15
Big Bend Unit 2 Compliance SO2 Data 

Date Time SO21 CO21

04/02/2008 8:52 30.1 9.2

04/02/2008 8:53 27.7 9.3

04/02/2008 8:54 26.6 9.3

04/02/2008 8:55 26.1 9.3

04/02/2008 8:56 25.6 9.3

04/02/2008 8:57 24.6 9.3

04/02/2008 8:58 24.4 9.4

04/02/2008 8:59 24.1 9.4

04/02/2008 9:00 24.2 9.3

04/02/2008 9:01 24 9.3

04/02/2008 9:02 23.6 9.3

04/02/2008 9:03 23.8 9.4

04/02/2008 9:04 24.2 9.5

04/02/2008 9:05 24.3 9.5

04/02/2008 9:06 24.4 9.5

04/02/2008 9:07 24 9.5

04/02/2008 9:08 24.1 9.5

04/02/2008 9:09 24.3 9.5

04/02/2008 9:10 25.8 9.4

04/02/2008 9:11 26.2 9.4

04/02/2008 9:12 26.1 9.4

04/02/2008 9:13 28.2 9.6

04/02/2008 9:14 30.2 9.8

04/02/2008 9:15 29 9.8

04/02/2008 9:16 26.2 9.7

04/02/2008 9:17 24.1 9.7

04/02/2008 9:18 24.4 9.5

04/02/2008 9:19 23.4 9.5

04/02/2008 9:20 21.8 9.4

04/02/2008 9:21 22.6 9.6

04/02/2008 9:22 22.9 9.6

04/02/2008 9:23 23.3 9.7

04/02/2008 9:24 22.9 9.7

04/02/2008 9:25 23.1 9.7

04/02/2008 9:26 23.4 9.7

04/02/2008 9:27 23.7 9.6

04/02/2008 9:28 24.2 9.5

Page 3 of 15
Big Bend Unit 2 Compliance SO2 Data 

Date Time SO21 CO21

04/02/2008 9:29 23.5 9.5

04/02/2008 9:30 25 9.6

04/02/2008 9:31 24.4 9.7

04/02/2008 9:32 24.5 9.7

04/02/2008 9:33 25.3 9.7

04/02/2008 9:34 25.2 9.8

04/02/2008 9:35 25.4 9.7

04/02/2008 9:36 25.7 9.7

04/02/2008 9:37 26.6 9.6

04/02/2008 9:38 27.1 9.6

04/02/2008 9:39 25.9 9.7

04/02/2008 9:40 26.1 9.7

04/02/2008 9:41 23.7 9.9

04/02/2008 9:42 21.4 9.9

04/02/2008 9:43 22.7 9.9

04/02/2008 9:44 23.4 9.8

04/02/2008 9:45 22.9 9.7

04/02/2008 9:46 23.7 9.7

04/02/2008 9:47 24 9.6

04/02/2008 9:48 23.7 9.7

04/02/2008 9:49 23.5 9.7

04/02/2008 9:50 22.1 9.8

04/02/2008 9:51 23 9.8

04/02/2008 9:52 22.7 9.8

04/02/2008 9:53 23.1 9.8

04/02/2008 9:54 23 9.7

04/02/2008 9:55 22.9 9.6

04/02/2008 9:56 23.7 9.7

04/02/2008 9:57 25 9.7

04/02/2008 9:58 24.9 9.7

04/02/2008 9:59 24.6 9.7

04/02/2008 10:00 24.7 9.7

04/02/2008 10:01 25.8 9.8

04/02/2008 10:02 25.5 9.8

04/02/2008 10:03 25.6 9.8

04/02/2008 10:04 24.5 9.8

04/02/2008 10:05 23.5 9.7

Page 4 of 15
Big Bend Unit 2 Compliance SO2 Data 

Date Time SO21 CO21

04/02/2008 10:06 22.3 9.7

04/02/2008 10:07 22.4 9.7

04/02/2008 10:08 22.4 9.8

04/02/2008 10:09 22.2 9.7

04/02/2008 10:10 23.6 9.7

04/02/2008 10:11 24.2 9.7

04/02/2008 10:12 25 9.7

04/02/2008 10:13 25.6 9.6

04/02/2008 10:14 24.9 9.7

04/02/2008 10:15 26.4 9.8

04/02/2008 10:16 25.5 9.7

04/02/2008 10:17 24.2 9.6

04/02/2008 10:18 25.1 9.6

04/02/2008 10:19 25.9 9.6

04/02/2008 10:20 25.5 9.7

04/02/2008 10:21 26.2 9.7

04/02/2008 10:22 25.9 9.6

04/02/2008 10:23 26.1 9.6

04/02/2008 10:24 26.9 9.7

04/02/2008 10:25 28.4 9.7

04/02/2008 10:26 27.6 9.8

04/02/2008 10:27 27.1 9.8

04/02/2008 10:28 27.7 9.8

04/02/2008 10:29 24.6 9.6

04/02/2008 10:30 23.5 9.6

04/02/2008 10:31 23.2 9.6

04/02/2008 10:32 22.9 9.6

04/02/2008 10:33 23.2 9.5

04/02/2008 10:34 22.4 9.5

04/02/2008 10:35 24.4 9.7

04/02/2008 10:36 25.2 9.8

04/02/2008 10:37 26.3 9.8

04/02/2008 10:38 24.5 9.6

04/02/2008 10:39 24.6 9.7

04/02/2008 10:40 25.8 9.7

04/02/2008 10:41 26.5 9.7

04/02/2008 10:42 25.3 9.6

Page 5 of 15
Big Bend Unit 2 Compliance SO2 Data 

Date Time SO21 CO21

04/02/2008 10:43 26.7 9.6

04/02/2008 10:44 25.4 9.7

04/02/2008 10:45 25.1 9.8

04/02/2008 10:46 28.9 9.8

04/02/2008 10:47 28.7 9.6

04/02/2008 10:48 28.6 9.6

04/02/2008 10:49 29.5 9.8

04/02/2008 10:50 28 9.8

04/02/2008 10:51 26.5 9.8

04/02/2008 10:52 24.9 9.8

04/02/2008 10:53 23.1 9.7

04/02/2008 10:54 23.7 9.6

04/02/2008 10:55 24.8 9.7

04/02/2008 10:56 23.3 9.9

04/02/2008 10:57 23.1 9.9

04/02/2008 10:58 22.8 9.7

04/02/2008 10:59 22.7 9.7

04/02/2008 11:00 22.8 9.6

04/02/2008 11:01 23.6 9.7

04/02/2008 11:02 22.9 9.6

04/02/2008 11:03 23.6 9.7

04/02/2008 11:04 23.3 9.7

04/02/2008 11:05 23.4 9.6

04/02/2008 11:06 24.1 9.7

04/02/2008 11:07 24.8 9.8

04/02/2008 11:08 25.2 9.9

04/02/2008 11:09 25.2 9.7

04/02/2008 11:10 25.2 9.6

04/02/2008 11:11 25.4 9.6

04/02/2008 11:12 25.4 9.7

04/02/2008 11:13 25.4 9.7

04/02/2008 11:14 25.4 9.8

04/02/2008 11:15 25.1 9.9

04/02/2008 11:16 24.6 9.9

04/02/2008 11:17 23.4 10

04/02/2008 11:18 22.7 10

04/02/2008 11:19 21.9 9.9

Page 6 of 15
Big Bend Unit 2 Compliance SO2 Data 

Date Time SO21 CO21

04/02/2008 11:20 20.8 9.8

04/02/2008 11:21 21.1 9.7

04/02/2008 11:22 21 9.8

04/02/2008 11:23 21.2 9.9

04/02/2008 11:24 21.3 9.9

04/02/2008 11:25 21.9 9.9

04/02/2008 11:26 21.9 9.9

04/02/2008 11:27 22.2 9.9

04/02/2008 11:28 23 9.9

04/02/2008 11:29 22.7 9.9

04/02/2008 11:30 22.6 9.8

04/02/2008 11:31 23.1 9.8

04/02/2008 11:32 23.4 9.8

04/02/2008 11:33 24.2 9.8

04/02/2008 11:34 24.5 9.8

04/02/2008 11:35 24.8 9.8

04/02/2008 11:36 25.4 9.9

04/02/2008 11:37 25.2 10

04/02/2008 11:38 24.8 9.9

04/02/2008 11:39 24.2 9.9

04/02/2008 11:40 23.5 10

04/02/2008 11:41 22.5 10.1

04/02/2008 11:42 21.2 9.9

04/02/2008 11:43 20.9 9.8

04/02/2008 11:44 21.4 9.8

04/02/2008 11:45 22 9.9

04/02/2008 11:46 22.6 10

04/02/2008 11:47 21.3 10

04/02/2008 11:48 20.9 9.9

04/02/2008 11:49 22 9.8

04/02/2008 11:50 22.6 9.7

04/02/2008 11:51 23.7 9.9

04/02/2008 11:52 23.5 9.9

04/02/2008 11:53 23.5 9.8

04/02/2008 11:54 23.8 9.9

04/02/2008 11:55 24.5 10

04/02/2008 11:56 24.8 10.1

Page 7 of 15
Big Bend Unit 2 Compliance SO2 Data 

Date Time SO21 CO21

04/02/2008 11:57 25.2 10.1

04/02/2008 11:58 25.5 10

04/02/2008 11:59 25.5 10

04/02/2008 12:00 25.7 10

04/02/2008 12:01 27.6 9.9

04/02/2008 12:02 29 9.9

04/02/2008 12:03 28 10

04/02/2008 12:04 27.7 10.2

04/02/2008 12:05 26.3 10.1

04/02/2008 12:06 25.4 10.1

04/02/2008 12:07 25.5 10

04/02/2008 12:08 26 9.9

04/02/2008 12:09 26.3 9.9

04/02/2008 12:10 26.9 9.9

04/02/2008 12:11 27.2 9.8

04/02/2008 12:12 27 9.8

04/02/2008 12:13 27.4 9.8

04/02/2008 12:14 27.8 10

04/02/2008 12:15 27.9 10.1

04/02/2008 12:16 27.5 10

04/02/2008 12:17 27.8 9.9

04/02/2008 12:18 28.7 9.9

04/02/2008 12:19 30 9.9

04/02/2008 12:20 31.1 10

04/02/2008 12:21 31.1 10

04/02/2008 12:22 31.2 10.1

04/02/2008 12:23 31.2 10.1

04/02/2008 12:24 31.4 10.2

04/02/2008 12:25 29.8 10.3

04/02/2008 12:26 28.5 10.2

04/02/2008 12:27 27.1 10.1

04/02/2008 12:28 26.2 10.1

04/02/2008 12:29 27 10.1

04/02/2008 12:30 26.7 10

04/02/2008 12:31 24.9 9.9

04/02/2008 12:32 24.8 10.1

04/02/2008 12:33 25 10.2

Page 8 of 15
Big Bend Unit 2 Compliance SO2 Data 

Date Time SO21 CO21

04/02/2008 12:34 25.8 10.2

04/02/2008 12:35 25.9 10.2

04/02/2008 12:36 25.6 10.2

04/02/2008 12:37 26.1 10.2

04/02/2008 12:38 25.5 10.1

04/02/2008 12:39 25.8 10

04/02/2008 12:40 25.7 9.9

04/02/2008 12:41 26.1 10

04/02/2008 12:42 26.6 10

04/02/2008 12:43 27 10.1

04/02/2008 12:44 27.6 10.2

04/02/2008 12:45 27.5 10.3

04/02/2008 12:46 27.8 10.2

04/02/2008 12:47 26.3 10.2

04/02/2008 12:48 25.2 10.2

04/02/2008 12:49 24.4 10.2

04/02/2008 12:50 22.6 10.1

04/02/2008 12:51 22.7 10.2

04/02/2008 12:52 24 10.2

04/02/2008 12:53 23.4 10.2

04/02/2008 12:54 23.7 10.1

04/02/2008 12:55 23.8 10.1

04/02/2008 12:56 24.3 10

04/02/2008 12:57 25.2 10.2

04/02/2008 12:58 25.8 10.1

04/02/2008 12:59 24.6 9.9

04/02/2008 13:00 24.4 9.8

04/02/2008 13:01 25.6 9.8

04/02/2008 13:02 25.6 9.9

04/02/2008 13:03 26.6 9.9

04/02/2008 13:04 26.4 9.8

04/02/2008 13:05 26.6 9.9

04/02/2008 13:06 27.9 10.1

04/02/2008 13:07 28.8 10.2

04/02/2008 13:08 27.7 10.3

04/02/2008 13:09 26.4 10.2

04/02/2008 13:10 25.4 10.1

Page 9 of 15
Big Bend Unit 2 Compliance SO2 Data 

Date Time SO21 CO21

04/02/2008 13:11 24.6 10.1

04/02/2008 13:12 23.7 10

04/02/2008 13:13 23.9 10.1

04/02/2008 13:14 24.3 10.1

04/02/2008 13:15 24.8 10.1

04/02/2008 13:16 24.5 10.2

04/02/2008 13:17 24.2 10.2

04/02/2008 13:18 24.5 10.1

04/02/2008 13:19 25.1 10

04/02/2008 13:20 24.2 9.9

04/02/2008 13:21 26.8 9.9

04/02/2008 13:22 27.7 9.9

04/02/2008 13:23 27.2 10

04/02/2008 13:24 29.9 10

04/02/2008 13:25 31.2 10.1

04/02/2008 13:26 30.6 10.1

04/02/2008 13:27 32.2 10.2

04/02/2008 13:28 32.5 10.2

04/02/2008 13:29 31.1 10.1

04/02/2008 13:30 31.3 10

04/02/2008 13:31 28.3 10

04/02/2008 13:32 27.4 10

04/02/2008 13:33 28.1 10.1

04/02/2008 13:34 28.1 10.1

04/02/2008 13:35 26.5 10.2

04/02/2008 13:36 25.6 10.1

04/02/2008 13:37 24.9 9.9

04/02/2008 13:38 24.7 9.9

04/02/2008 13:39 25.8 9.9

04/02/2008 13:40 26 9.9

04/02/2008 13:41 25.2 9.9

04/02/2008 13:42 26 9.9

04/02/2008 13:43 26.4 9.9

04/02/2008 13:44 26.9 9.9

04/02/2008 13:45 27.2 10

04/02/2008 13:46 28.1 10

04/02/2008 13:47 27 9.9

Page 10 of 15
Big Bend Unit 2 Compliance SO2 Data 

Date Time SO21 CO21

04/02/2008 13:48 26.9 9.8

04/02/2008 13:49 27.5 9.9

04/02/2008 13:50 27.8 9.8

04/02/2008 13:51 29.1 10

04/02/2008 13:52 29 10

04/02/2008 13:53 26 10

04/02/2008 13:54 25.5 10.1

04/02/2008 13:55 27.6 10.2

04/02/2008 13:56 26.6 10.2

04/02/2008 13:57 25.4 10.1

04/02/2008 13:58 24.6 10.1

04/02/2008 13:59 25.1 10.2

04/02/2008 14:00 24.7 10.2

04/02/2008 14:01 24.7 10.2

04/02/2008 14:02 24.5 10.1

04/02/2008 14:03 24.4 10

04/02/2008 14:04 24.8 9.9

04/02/2008 14:05 25.7 10

04/02/2008 14:06 27 10.1

04/02/2008 14:07 29 10.1

04/02/2008 14:08 27.7 10.1

04/02/2008 14:09 26.9 10

04/02/2008 14:10 26.9 9.9

04/02/2008 14:11 28.9 10

04/02/2008 14:12 29.2 10.1

04/02/2008 14:13 28.5 10.1

04/02/2008 14:14 28.3 10.1

04/02/2008 14:15 27.8 10

04/02/2008 14:16 27.8 10

04/02/2008 14:17 27.4 10.1

04/02/2008 14:18 26.5 10.1

04/02/2008 14:19 25 10.1

04/02/2008 14:20 23.7 10

04/02/2008 14:21 24 10.1

04/02/2008 14:22 24.2 10.2

04/02/2008 14:23 23.7 10.1

04/02/2008 14:24 24.1 10.1

Page 11 of 15
Big Bend Unit 2 Compliance SO2 Data 

Date Time SO21 CO21

04/02/2008 14:25 25 10.1

04/02/2008 14:26 24.7 10

04/02/2008 14:27 24.8 10

04/02/2008 14:28 25.5 10

04/02/2008 14:29 25.5 10

04/02/2008 14:30 25.9 10

04/02/2008 14:31 25.9 9.9

04/02/2008 14:32 26.2 9.9

04/02/2008 14:33 26.3 9.9

04/02/2008 14:34 28.1 10

04/02/2008 14:35 30.1 10.1

04/02/2008 14:36 29.7 10

04/02/2008 14:37 29 10

04/02/2008 14:38 29.6 10

04/02/2008 14:39 30.3 10.1

04/02/2008 14:40 28.8 10.2

04/02/2008 14:41 27.1 10.1

04/02/2008 14:42 27.1 10

04/02/2008 14:43 25.8 10

04/02/2008 14:44 25.7 10

04/02/2008 14:45 25.7 10.1

04/02/2008 14:46 26.6 10

04/02/2008 14:47 26.1 10

04/02/2008 14:48 26.2 10

04/02/2008 14:49 26.5 10.1

04/02/2008 14:50 26.6 10.1

04/02/2008 14:51 25.5 10.1

04/02/2008 14:52 25.3 9.9

04/02/2008 14:53 23.5 9.9

04/02/2008 14:54 23 9.8

04/02/2008 14:55 24.6 9.8

04/02/2008 14:56 23.1 9.9

04/02/2008 14:57 23.9 9.9

04/02/2008 14:58 26.2 9.9

04/02/2008 14:59 25.2 10

04/02/2008 15:00 26.8 10.1

04/02/2008 15:01 28.4 10.2

Page 12 of 15
Big Bend Unit 2 Compliance SO2 Data 

Date Time SO21 CO21

04/02/2008 15:02 26.7 10.1

04/02/2008 15:03 24.8 9.9

04/02/2008 15:04 24.5 9.8

04/02/2008 15:05 22.4 9.8

04/02/2008 15:06 22 9.9

04/02/2008 15:07 21.8 9.8

04/02/2008 15:08 21.7 9.9

04/02/2008 15:09 22.8 10

04/02/2008 15:10 22.8 9.9

04/02/2008 15:11 22.3 9.9

04/02/2008 15:12 23.1 10

04/02/2008 15:13 23.5 10

04/02/2008 15:14 24.1 10

04/02/2008 15:15 24 10

04/02/2008 15:16 24.2 9.9

04/02/2008 15:17 26.9 10

04/02/2008 15:18 27.3 9.9

04/02/2008 15:19 26.1 9.8

04/02/2008 15:20 26.5 9.8

04/02/2008 15:21 25.9 10

04/02/2008 15:22 25.3 10

04/02/2008 15:23 25.2 9.9

04/02/2008 15:24 25.5 9.9

04/02/2008 15:25 25.7 9.9

04/02/2008 15:26 24.2 9.9

04/02/2008 15:27 22.9 9.8

04/02/2008 15:28 22.6 9.8

04/02/2008 15:29 22.6 10

04/02/2008 15:30 23.6 10.1

04/02/2008 15:31 24 10.1

04/02/2008 15:32 23.1 10.3

04/02/2008 15:33 24.9 10.4

04/02/2008 15:34 25.6 10.4

04/02/2008 15:35 25.3 10.3

04/02/2008 15:36 25.1 10.2

04/02/2008 15:37 25.6 10

04/02/2008 15:38 25.7 10.1

Page 13 of 15
Big Bend Unit 2 Compliance SO2 Data 

Date Time SO21 CO21

04/02/2008 15:39 25.9 10

04/02/2008 15:40 26.6 9.9

04/02/2008 15:41 25.3 9.8

04/02/2008 15:42 26.1 9.8

04/02/2008 15:43 26.8 9.9

04/02/2008 15:44 26 9.8

04/02/2008 15:45 24.8 9.7

04/02/2008 15:46 26 9.7

04/02/2008 15:47 27.6 9.7

04/02/2008 15:48 25.4 9.8

04/02/2008 15:49 24.2 9.8

04/02/2008 15:50 24 9.7

04/02/2008 15:51 23.2 9.7

04/02/2008 15:52 22.6 9.7

04/02/2008 15:53 21.8 9.7

04/02/2008 15:54 22.7 9.8

04/02/2008 15:55 23.8 9.9

04/02/2008 15:56 23 10

04/02/2008 15:57 22.8 9.8

04/02/2008 15:58 23.3 9.8

04/02/2008 15:59 21.1 9.8

04/02/2008 16:00 21.1 9.9

04/02/2008 16:01 23.2 9.8

04/02/2008 16:02 23.2 9.6

04/02/2008 16:03 23.7 9.6

04/02/2008 16:04 25.2 9.6

04/02/2008 16:05 24.1 9.7

04/02/2008 16:06 25.1 9.7

04/02/2008 16:07 26.6 9.7

04/02/2008 16:08 24.5 9.7

04/02/2008 16:09 25.9 9.8

04/02/2008 16:10 26.3 9.9

04/02/2008 16:11 25.7 9.9

04/02/2008 16:12 23.9 9.8

04/02/2008 16:13 22.7 9.7

04/02/2008 16:14 22.1 9.7

04/02/2008 16:15 21.9 9.8

Page 14 of 15
Big Bend Unit 2 Compliance SO2 Data 

Date Time SO21 CO21

04/02/2008 16:16 21.7 9.7

04/02/2008 16:17 21.7 9.8

04/02/2008 16:18 22.7 9.9

04/02/2008 16:19 22.9 10

04/02/2008 16:20 23.1 9.9

04/02/2008 16:21 22.7 9.9

04/02/2008 16:22 22.9 9.8

Averages: 24.88 9.83

Page 15 of 15
APPENDIX E

FUEL ANALYSIS 
Laboratory Services

5012 Causeway Blvd * Tampa Fl. 33619 

 Ph (813) 630-7378 * Fax (813) 630-7360 * DOH #E54272

Report For: 05/08/2008

Location Code: TE_BB_2_COMP_CO

Location Description:

Sample Collector:

Sample Collection Date:

Lab Submittal Date:

Sample Information

Big Bend 2 Compliance 04/02/2008

04/03/2008

F. WADE

Report Date:

Laboratory ID: AA93807

Laboratory Results

Coal Analysis - As Received Result Units

Lower

Limit

Upper

Limit Violation

Ash, as Received 10.54 %

BTU, as Received 11803 BTU/Lb

Sulfur, as Received 1.62 %

Coal Analysis - Dry Basis Result Units

Lower

Limit

Upper

Limit Violation

Ash, Dry Basis 11.67 %

BTU, Dry Basis 13062 BTU/Lb.

Sulfur, Dry Basis 1.79 %

Coal Analysis - Miscellaneous Result Units

Lower

Limit

Upper

Limit Violation

BTU, Moisture-Ash Free 14788 BTU/Lb.

Pounds SO2 / Million BTU 2.61 Lbs. SO2/MMBTU

Total Moisture 9.64 %

Comments

Ray McDarby,

Manager, Laboratory Services

For Peggy Penner,

Report Number: -050808- 08 AA93807 Page 1 of 1 "Coal Report"
APPENDIX F

FIELD DATA SHEETS 






APPENDIX G

SAMPLING EQUIPMENT CALIBRATIONS 
Environmental Services

Air Services Group

SUMMARY OF EQUIPMENT CALIBRATIONS

EQUIPMENT CAL DATE METHOD RESULTS

CONSOLE (MB 06)

INITIAL 02/01/2008 USEPA RM 5 0.998

POST TEST 04/03/2008 (ORIFICE) 0.994

NOZZLE (MN 19)

INITIAL 02/01/2008 CALIPER 0.279

POST TEST 04/03/2008 CALIPER 0.280

PYROMETER (PY 10) 02/01/2008 ASTM THERMOMETER + 2o

 F

PITOT TUBE (PT 09) 02/01/2008 USEPA RM 2 Cp = 0.84

BAROMETER (BR 07) 03/03/2008 NWS COMPARISON + 0.01" Hg
Environmental Services

Air Services Group

Red Team

Manufacturer: Thermo Anderson Calibration Date:

Model Number:MST-C1 Barometric Pressure: 30.14 "Hg

Instrument Code Number: ^MB06 Theoretical Critical Vacuum: 14.22 "Hg

LabWorks Sample Number: Calibrated By:

Initial Final Total

ΔH Time Volume Volume Volume Inlet Outlet Inlet Outlet

"H2O Minutes ft3 ft3 ft3

oF oF oF oF

0.60 15 535.666 542.550 6.884 77 81 80 82

1.15 15 509.900 518.920 9.020 77 79 78 81

1.95 15 524.000 535.666 11.666 78 81 77 82

3.70 15 542.463 558.450 15.987 80 82 74 81

Orifice K' Actual

Serial Orifice Vacuum Initial Final Average

Number Coefficient "Hg oF oF oF

48 0.3455 23.0 72 72 72.0

55 0.4592 21.5 72 72 72.0

63 0.5877 19.7 72 72 72.0

73 0.8022 16.9 72 72 72.0

Dry Gas Meter Calibration Calibration

Volume Volume Volume Y ΔHα

Corrected Corrected Nominal Value QA/QC Value QA/QC

Vm(std), ft3 Vcr(std), ft3 Vcr(std), ft3 (ratio) + 0.02 "H2O + 0.2

6.788 6.772 6.776 0.998 0.000 1.631 -0.146

8.926 9.001 9.006 1.008 0.010 1.774 -0.003

11.551 11.520 11.527 0.997 -0.001 1.834 0.057

15.905 15.724 15.734 0.989 -0.009 1.868 0.092

Averages: 0.998 1.777

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 ΔHα, the acceptable tolerance of individual values from the average is + 0.2.

4-Feb-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

02/01/2008

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: 30.15 "Hg

Instrument Code Number: mb06 Theoretical Critical Vacuum: 14.22 "Hg

LabWorks Sample Number: Calibrated By:

Associated Test: Team: RED

Initial Final Total

ΔH Time Volume Volume Volume Inlet Outlet Inlet Outlet

"H2O Minutes ft3 ft3 ft3

oF oF oF oF

1.2 10 119.000 125.020 6.020 68 74 69 75

1.2 10 125.020 131.040 6.020 69 75 69 76

1.2 10 131.040 137.075 6.035 69 76 70 77

Orifice K' Actual

Serial Orifice Vacuum Initial Final Average

Number Coefficient "Hg oF oF oF

55 0.4593 23.0 72 72 72.0

55 0.4593 23.0 72 72 72.0

55 0.4593 23.0 72 72 72.0

Dry Gas Meter Calibration Calibration

Volume Volume Volume Y ΔHα

Corrected Corrected Nominal Value QA/QC Value QA/QC

Vm(std), ft3 Vcr(std), ft3 Vcr(std), ft3 (ratio) + 0.02 "H2O + 0.2

6.042 6.004 6.006 0.994 -0.001 1.875 0.003

6.033 6.004 6.006 0.995 0.001 1.872 0.000

6.040 6.004 6.006 0.994 0.000 1.869 -0.003

Averages: 0.994 1.872

Prior Y: 0.998

% Difference: 0.37% + 5%

Review/Approval: Date: 4-Apr-08

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 ΔHα, the acceptable tolerance of individual values from the average is + 0.2.

Critical Orifice

USEPA Reference Method 5

Dry Gas Meter Calibration

Critical Orifice Method

rjn

04/03/2008

POST - TEST CALIBRATION CHECK

Ambient Temperatures

Dry Gas Meter Readings

Initial Temperatures Final Tempertures

Critical Orifice Readings

BIG BEND UNIT 2-04-02-08

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.
Environmental Services

Air Services Group

QUARTERLY NOZZLE CALIBRATIONS

Shared Resource

STEEL NOZZLE SET

Calibration Date: 02/01/2008 Responsible Party: RJN

Nozzle Nozzle Diameter, Dn (cm) Maximum Average

I.D. D1 D2 D3 Difference, " Dn, inches

^SN01 0.292 0.286 0.293 0.003 0.114

^SN04 0.322 0.323 0.323 0.000 0.127

^SN05 0.379 0.380 0.378 0.001 0.149

^SN06 0.494 0.496 0.499 0.002 0.195

^SN09 0.686 0.689 0.686 0.001 0.270

^SN10 0.754 0.750 0.750 0.002 0.296

^SN12 0.985 0.979 0.982 0.002 0.387

^SN15 0.419 0.416 0.414 0.002 0.164

^SN16 0.501 0.501 0.499 0.001 0.197

^SN19 0.711 0.706 0.712 0.002 0.279

^SN22 0.934 0.935 0.932 0.001 0.368

^SN30 0.792 0.792 0.794 0.001 0.312

^SN36 0.467 0.474 0.473 0.003 0.186

^SN37 0.527 0.530 0.533 0.002 0.209

^SN38 0.628 0.632 0.633 0.002 0.248

^SN46 0.479 0.479 0.478 0.000 0.188

^SN47 0.514 0.511 0.508 0.002 0.201

^SN48 0.636 0.638 0.634 0.002 0.250

^SN50 0.788 0.784 0.784 0.002 0.309

^SN58 0.610 0.616 0.618 0.003 0.242

^SN68 0.622 0.625 0.625 0.001 0.246

^SN69 0.950 0.950 0.951 0.000 0.374

^SN70 1.561 1.558 1.553 0.003 0.613

^SN71 1.554 1.557 1.555 0.001 0.612

^SN72 0.953 0.954 0.950 0.002 0.375

^SN73 1.280 1.280 1.280 0.000 0.504

^SN74 1.230 1.231 1.230 0.000 0.484

Data Notations: All micometer readings are converted from cm to inches by multiplying by

0.393700787. Maximum Difference must be < 0.004".

QA/QC Review by:
Environmental Services

Air Services Group

POST TEST NOZZLE CALIBRATION 

Shared Resource

Calibration Date: 04/03/2008

Calibration Personnel: rjn

Test Designation: big bend unit 2 04-02-08

Nozzle Nozzle Diameter, Dn (cm) Maximum Average

Identifier D1 D2 D3 Difference, " Dn, inches

sn19 0.710 0.708 0.712 0.002 0.280

Data Notations: All micometer readings are converted from cm to inches by multiplying by

0.393700787. Maximum Difference must be < 0.004".

Quarterly (pre-test) value for nozzle ID sn19 was 0.279

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

4-Apr-08

QA/QC Review by:
Environmental Services

Air Services Group

Pyrometer Calibration

Red Team

Pyrometer Under Test

Pyrometer Number: ^PY10

Labworks Sample # 0

Calibration Date: 02/01/2008

Calibrator Information

Calibrator Type/Manufacturer: Hart Scientific

Calibrator Serial Number: AOA024

Date of Last Calibration: 04/17/2007

Calibration Personnel (Typed and Signature): SEG-RJN

Calibration Data

Calibration Reference Pyrometer

Point Temperature Indication Difference

1 400 401 -1

2 212 214 -2

3 32 34 -2

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: 4-Feb-08
Environmental Services

Air Services Group

_ _

s

PITOT TUBE CALIBRATION

DATA SHEET

Pitot Tube ID # PT09

Calibration Date 02/01/2008 Operating Quarter/Year: 1/08 Shared Resource

Openings Damaged? ___ Y __ N Repaired? ___ Y ___ N ___ N/A

Labworks #: 0

Alpha and Beta Angle Determinations Acceptable Limits:

α 1 1.9 degrees Pass Dt 0.48 < Dt > 0.95 cm

α 2 1.1 degrees Pass α < 10 degrees

β 1 1.6 degrees Pass (α1 measured across top impact openings)

β 2 1.8 degrees Pass (α2 measured across bottom impact openings)

β1 < 5 degrees (alongside top impact openings)

Gamma, Theta, Α, Ζ, and W Determination β2 < 5 degrees (alongside bottom impact openings)

ψ 0.1 degrees Ζ < 0.32 cm (Αsinψ)

Α 2.28 cm W < 0.08 cm (Asinο)

Ζ 0.004 cm Pass Α distance between tips

ο angle of plane on side of pitots

ο 0.3 degrees ψ angle between tips

W 0.012 cm 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.

Comments: REMOVABLE

Calibrated by: RJN - SEG

Quality Assurance Review / Approval:
Environmental Services

Air Services Group

BAROMETER CALIBRATION

Blue Team

Instrument Number: ^BR07

Calibration Date: 03/03/2008

Calibration Personnel: SEG

Labworks #:

Barometer Reading Reference Reading Difference

Time Inches Mercury Inches Mercury "Hg

9:00 29.98 29.99 -0.01

10:00 29.99 30.00 -0.01

11:00 30.01 30.01 0

Average Difference: -0.00667

Note: Barometric readings must agree within ± 0.1 "Hg.

Current Reference is National Weather Service, TIA.

Current Conditions at Tampa International Airport

Comments (Note any adjustments):

QA/QC Review by: Date: 5-Mar-08
APPENDIX H

CHAIN OF CUSTODY 

APPENDIX I

TEST PARTICIPANTS 
TEST PARTICIPANTS

ENVIRONMENTAL SERVICES 

AIR SERVICES GROUP

Test Team

Jorge Varino Environmental Technician, Test Team Lead 

Gary Barber Associate Technician 

Scott Given Associate Technician 

Ryan Newell Associate Technician 

Process Data

Karen Zwolak Senior Environmental Consultant, Big Bend Station 

Raymond A. McDarby Senior Environmental Technician 

Fuel Analysis

Patrice Jackson Environmental Technician 

Sample Analysis

Sam Soth Environmental Technician 

Project Quality Objectives & Reporting

Raymond A. McDarby Senior Environmental Technician 

Test Coordination

Karen Zwolak Senior Environmental Consultant, Big Bend Station 

David A. Smith Coordinator, Air Services Group