COMPLIANCE TEST REPORT 

BIG BEND STATION 

FACILITY ID NUMBER: 0570039 

EMISSION UNIT ID NO: -003 

PARTICULATE MATTER, SULFUR DIOXIDE, 

AND, 

VISIBLE EMISSIONS EVALUATION 

February 25, 2005 

Prepared For: 

Tampa Electric Company 

Polk Power 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 

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 

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

were conducted at my direction, and I hereby certify that this test report is 

authentic and accurate to the best of my knowledge. 

Signature:__________________________ 

Charles R. Dufeny 

Environmental Technician 

Test Team Lead 

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

1.0 INTRODUCTION 1 

2.0 DISCUSSION OF RESULTS 2 

3.0 SOURCE DESCRIPTION/TEST PROCEDURES 3 

4.0 TEST RESULTS 

 PARTICULATE TEST SUMMARY (SOOT BLOWING) 6 

 PARTICULATE TEST SUMMARY (NON-SOOT BLOWING) 7 

 SULFUR DIOXIDE DATA SUMMARY 8 

 VISIBLE EMISSIONS DATA SUMMARY (SOOT BLOWING) 9 

 VISIBLE EMISSIONS DATA SUMMARY (NON-SOOT BLOWING) 10 

 HEAT INPUT AND FUEL CONSUMPTION SUMMARY 11 

5.0 FIGURES 

SAMPLING LOCATION DIAGRAM 13 

APPENDICIES

 A PARTICULTE TEST CALCULATIONS 

 B DAILY SULFUR DIOXIDE DATA SUMMARY 

 C PARTICULATE LABORATORY ANALYTICAL DATA 

 D BOILER/PRECIPITATOR OPERATIONAL DATA 

 E FUEL ANALYSIS 

 F FIELD DATA SHEETS 

 G SAMPLING EQUIPMENT CALIBRATIONS 

 H CHAIN OF CUSTODY 

 I TEST PARTICIPANTS 
1 

1.0 INTRODUCTION

On February 25, 2005, the Environmental Services, Air Services Group of Tampa 

Electric Company, performed source emission tests at the Big Bend Station, 

Boiler No. 3, emissions unit I.D.# 0570039-003. Testing was conducted 

according to procedures stipulated by the Florida Department of Environmental 

Protection (FDEP) for fossil fuel steam generators, and requirements in Title V 

Permit # 0570039-021-AV. 
2 

2.0 DISCUSSION OF RESULTS

The particulate matter emission rate under sootblowing conditions was derived 

from three United States Environmental Protection Agency (USEPA) Reference 

Method 5-B test runs. The average of the three test runs was 0.02 lb/mmBtu. 

The FDEP allowable emission rate under soot blowing conditions is 0.03 

lb/MMBtu, as listed in condition A.7. 

The particulate matter emission rate under non-sootblowing conditions was 

derived from three USEPA Reference Method 5-B test runs. The average of the 

three test runs was 0.02 lb/MMBtu. The FDEP allowable emission rate under 

non-sootblowing conditions is 0.03 lb/MMBtu, as listed in condition A.7. 

The sulfur dioxide 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 1037 lbs/hr. The FDEP allowable emission rate is 3374 lbs/hr, 

based on scenario 3 as listed in condition A.9.e. 

Visible emissions were evaluated using a Teledyne Instruments/Monitor Labs, 

LightHawk 560 transmissometer system (S/N 5600448/5600446), during both 

sootblowing and non-sootblowing testing. The 1-hour average opacity under 

sootblowing conditions was 3.5%. The 1-hour average opacity under nonsootblowing conditions was 3.5%. The FDEP allowable emission rate is 20%, as 

listed in condition A.6. 

During the tests performed on February 25, 2005, Boiler No. 3 was operated at 

an average heat input rate of 3845 mmBtu/hr and an average load of 377 

megawatts. The average quantity of fuel burned was 160.4 tons per hour. 
3 

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 common stack 3 (CS003) source 

sampling location consists of a circular stack 28.83 feet in diameter with four 

sample ports located 90 degrees apart on the stack circumference. Upstream 

and downstream gas flow disturbances were determined to be 8.51 and 2.99 

stack diameters from the test ports, respectively. Using these criteria, a total of 

24 sampling points were chosen for particulate sampling, as stipulated in USEPA 

Method 1 – “Sample and Velocity Traverses for Stationary Sources”. A diagram 

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

information on the test site. 

Boiler No. 3 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. 

Particulate matter sampling was performed according to USEPA Method 5B 

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

Particulate matter was collected on a high purity, borosilicate microfiber filter 

measuring 82mm in diameter. This data is included as Appendix A, and 

summarized on pages 6 (soot blowing conditions), and 7 (non-soot blowing 

conditions) of this report. 

Diluent gas sampling and analysis was performed according to USEPA Method 3 

"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 System (DAHS). Averages were derived from the time frame of 09:12 

through 15:18 EST, corresponding to the time frame of the particulate matter 
4 

test. Data from 10:02 through 10:05 was not included in the averaging due to 

probe blowback (normal operations to ensure that the sampling system remains 

clean). This data is included as Appendix B, and summarized on page 8 of this 

report. 

Visible emissions were assessed using the installed Continuous Opacity Monitor 

(COM) system. This data is summarized on pages 9 (soot blowing conditions), 

and 10 (non-soot blowing conditions). 
5 

4.0 TEST RESULTS
BIG BEND STATION

PARTICULATE MATTER DATA SUMMARY

Run 1s Run 2s Run 3s

Vm(std), scf 38.486 38.267 38.111

Bws, ratio 0.11940 0.11914 0.13428

O2, % volume 8 8 5

Md, lb/lb - mole 30.56 30.56 30.28

Ms, lb/lb - mole 29.06 29.06 28.63

Qs, acf/min 1205845.8 1188859.2 1196891.6

Qs(std), dscf/min 939879.4 925152.9 913440.6

I, % 99.2 100.2 101.1

C, lbs/dscf 9.80E-07 1.13E-06 1.03E-06

Em, lbs/hr 55.24 63.00 56.43

Er, lb/mmBtu 0.0155 0.0180 0.0132

Mass emissions (Em), lbs/hr, calculated as: C x Qs(std) x 60 minutes/hour

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

100.17

1.0480E-06

58.223

0.01558

30.467

28.918

1197198.86

926157.66

Test Summary

38.288

0.124275

7.00

Boiler # 3

WET-BOTTOM UTILITY BOILER

February 25, 2005

SOOT BLOWING

6 
BIG BEND STATION

PARTICULATE MATTER DATA SUMMARY

Run 1 Run 2 Run 3

Vm(std), scf 37.136 36.643 37.961

Bws, ratio 0.12164 0.12159 0.13269

O2, % volume 8 8 8

Md, lb/lb - mole 30.56 30.56 30.56

Ms, lb/lb - mole 29.03 29.03 28.89

Qs, acf/min 1158800.3 1142896.5 1181548.1

Qs(std), dscf/min 901560.9 889030.0 909108.6

I, % 99.8 99.8 101.1

C, lbs/dscf 8.90E-07 1.05E-06 9.93E-07

Em, lbs/hr 48.17 56.16 54.17

Er, lb/mmBtu 0.0141 0.0167 0.0157

Mass emissions (Em), lbs/hr, calculated as: C x Qs(std) x 60 minutes/hour

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

9.7881E-07

52.833

0.01551

NON - SOOT BLOWING

28.986

1161081.64

899899.87

100.23

37.247

0.125309

8.00

30.560

Boiler # 3

WET-BOTTOM UTILITY BOILER

February 25, 2005

Test Summary

7 
BIG BEND STATION

SULFUR DIOXIDE DATA from CEMs

Test Period Information

Start Time 7:34:00 Eastern Standard Time (EST)

Stop Time 15:58:00 Eastern Standard Time (EST)

Total Time 8:24:00

Corresponding to the time frame for the PM test.

Sulfur Dioxide Data:

RM - 19

SO2 CO2 SO2 SO2

ppmvw %, wet lb/mmBtu lbs/hr

113.66946 12.61451 0.270 1037.45

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 = 3845 mmBtu/hr, from Heat Input Calculation

Boiler #3

WET-BOTTOM UTILITY BOILER

February 25, 2005

CEM DATA

8 
BIG BEND STATION

VISIBLE EMISSIONS DATA FROM OPACITY MONITOR

Record# DATE TIME OPACITY41Record# DATE TIME OPACITY41

1 02/25/2005 73400 3.500 31 02/25/2005 80400 3.300

2 02/25/2005 73500 3.600 32 02/25/2005 80500 3.300

3 02/25/2005 73600 3.500 33 02/25/2005 80600 3.300

4 02/25/2005 73700 3.800 34 02/25/2005 80700 3.100

5 02/25/2005 73800 3.600 35 02/25/2005 80800 3.200

6 02/25/2005 73900 3.800 36 02/25/2005 80900 3.200

7 02/25/2005 74000 3.200 37 02/25/2005 81000 3.300

8 02/25/2005 74100 2.900 38 02/25/2005 81100 3.800

9 02/25/2005 74200 3.200 39 02/25/2005 81200 3.800

10 02/25/2005 74300 3.300 40 02/25/2005 81300 3.600

11 02/25/2005 74400 3.300 41 02/25/2005 81400 3.400

12 02/25/2005 74500 3.600 42 02/25/2005 81500 3.500

13 02/25/2005 74600 3.400 43 02/25/2005 81600 3.800

14 02/25/2005 74700 3.300 44 02/25/2005 81700 3.700

15 02/25/2005 74800 3.000 45 02/25/2005 81800 3.500

16 02/25/2005 74900 3.000 46 02/25/2005 81900 3.600

17 02/25/2005 75000 3.200 47 02/25/2005 82000 3.500

18 02/25/2005 75100 3.800 48 02/25/2005 82100 3.500

19 02/25/2005 75200 3.700 49 02/25/2005 82200 3.600

20 02/25/2005 75300 3.500 50 02/25/2005 82300 3.900

21 02/25/2005 75400 3.400 51 02/25/2005 82400 3.500

22 02/25/2005 75500 3.500 52 02/25/2005 82500 3.400

23 02/25/2005 75600 3.400 53 02/25/2005 82600 3.700

24 02/25/2005 75700 3.700 54 02/25/2005 82700 3.500

25 02/25/2005 75800 3.800 55 02/25/2005 82800 3.800

26 02/25/2005 75900 3.400 56 02/25/2005 82900 3.600

27 02/25/2005 80000 3.600 57 02/25/2005 83000 3.000

28 02/25/2005 80100 3.300 58 02/25/2005 83100 3.300

29 02/25/2005 80200 3.300 59 02/25/2005 83200 3.200

30 02/25/2005 80300 3.300 60 02/25/2005 83300 3.200

Test Average: 3.450 %

Minimum One Minute Average: 2.900 %

Maximum One Minute Average: 3.900 %

Maximum Six Minute Average: 3.650 %

Boiler #3

WET BOTTOM UTILITY BOILER

SOOTBLOWING CONDITIONS

9 
BIG BEND STATION

VISIBLE EMISSIONS DATA FROM OPACITY MONITOR

Record# DATE TIME OPACITY41Record# DATE TIME OPACITY41

1 02/25/2005 90300 3.500 31 02/25/2005 93300 3.200

2 02/25/2005 90400 3.600 32 02/25/2005 93400 3.300

3 02/25/2005 90500 3.700 33 02/25/2005 93500 3.200

4 02/25/2005 90600 4.000 34 02/25/2005 93600 3.400

5 02/25/2005 90700 3.700 35 02/25/2005 93700 3.400

6 02/25/2005 90800 3.500 36 02/25/2005 93800 3.400

7 02/25/2005 90900 3.700 37 02/25/2005 93900 3.500

8 02/25/2005 91000 3.400 38 02/25/2005 94000 3.600

9 02/25/2005 91100 3.700 39 02/25/2005 94100 3.200

10 02/25/2005 91200 3.600 40 02/25/2005 94200 3.400

11 02/25/2005 91300 3.500 41 02/25/2005 94300 3.100

12 02/25/2005 91400 3.500 42 02/25/2005 94400 3.400

13 02/25/2005 91500 3.600 43 02/25/2005 94500 3.300

14 02/25/2005 91600 3.500 44 02/25/2005 94600 3.200

15 02/25/2005 91700 3.400 45 02/25/2005 94700 3.300

16 02/25/2005 91800 3.500 46 02/25/2005 94800 3.300

17 02/25/2005 91900 3.600 47 02/25/2005 94900 3.400

18 02/25/2005 92000 3.600 48 02/25/2005 95000 3.500

19 02/25/2005 92100 3.300 49 02/25/2005 95100 3.600

20 02/25/2005 92200 3.500 50 02/25/2005 95200 3.600

21 02/25/2005 92300 3.300 51 02/25/2005 95300 3.600

22 02/25/2005 92400 3.500 52 02/25/2005 95400 3.600

23 02/25/2005 92500 3.500 53 02/25/2005 95500 3.500

24 02/25/2005 92600 3.500 54 02/25/2005 95600 3.600

25 02/25/2005 92700 3.300 55 02/25/2005 95700 3.400

26 02/25/2005 92800 3.100 56 02/25/2005 95800 3.100

27 02/25/2005 92900 3.300 57 02/25/2005 95900 3.500

28 02/25/2005 93000 3.400 58 02/25/2005 100000 3.600

29 02/25/2005 93100 3.600 59 02/25/2005 100100 3.500

30 02/25/2005 93200 3.200 60 02/25/2005 100200 3.700

Test Average: 3.458 %

Minimum One Minute Average: 3.100 %

Maximum One Minute Average: 4.000 %

Maximum Six Minute Average: 3.700 %

Boiler #3

WET BOTTOM UTILITY BOILER

NON-SOOTBLOWING CONDITIONS

10 
BIG BEND GENERATING STATION

HEAT INPUT CALCULATIONS

Gross Heat Rate, Previous Month (January): 10193 KMBtu/MWh

1.0193E+07 MMBtu/MWh

MegaWatt Hour Integrator Information

Initial Integrator Reading: 304844 MWh

Final Integrator Reading: 308005 MWh

Total: 3161 MWh

Test Time Information

Testing Start Time: 7:35

Testing End Time: 15:58

Total Test Time: 8.38 hours

Calculated Heat Input

Average Unit Load, MW = MWh / hours: 377.2 MW

Heat Input, MMBtu/h = MMBtu/MWh x MW: 3844.8 mmBtu/hr

Fuel Consumption Calculation

Laboratory Sample ID: AA76139

Btu as received: 11986 Btu/lb

Tons of Fuel Consumed, Tons/hr = (mmBtu/h / Btu/lb) x 500: 160.4 Tons/hour

Coal Fired Boiler Number 3

February 25, 2005

11 
12 

5.0 FIGURES
FIGURE 1

EXHAUST STACK

245 FT.

BIG BEND STATION CS003

PARTICULATE TRAVERSE POINTS

OUTLET

N

A

B C

D

PORT LOCATION

REVISED 12-31-96

BOILER NO. 3 TEST LOCATION

STACK DIAMETERS DOWNSTREAM

FROM DISTURBANCE = 3.0

STACK DIAMETERS UPSTREAM

FROM DISTURBANCE = 8.5

STACK DIAMETER = 28.8333 FT.

STACK AREA = 652.948 SQ.

PORT LENGTH’S = 14 IN.

TRAVERSE

 POINT

 1

 2

 3

 4

 5

 6

 % OF

STACK DIAMETER

 IN. FROM

STACK WALL

 2.1%

 6.7%

11.8%

17.7%

25.0%

35.6%

 7.27 IN.

 23.18 IN.

 40.83 IN.

 61.24 IN.

 86.50 IN.

123.18 IN.

499 FT.

254 FT.

168 FT.

86 FT.

FGD

PRESSURIZED

 ANNULUS

13 
APPENDIX A 

PARTICULTE TEST CALCULATIONS 
Environmental Services

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: CS003 - Common Stack 3

Unit Under Test: Boiler # 3

Operating Conditions: Soot Blowing

Run Number: 1s

Date: 02/25/05

Sample Time, θ: 60 minutes Nozzle Diameter, Dn: 0.287 inches

Barometric Pressure, Pb: 29.75 "Hg Nozzle Area, An: 0.000449 ft2

Stack Pressure, Ps: 29.72 "Hg Average Orifice Meter, ∆H: 1.397 "H2O

Effective Stack Area, As: 652.948 ft2 Sample Volume, Vm: 39.897 ft3

Pitot Coefficient, Cp: 0.84 dimensionless Average Meter Temp., Tm: 86.7 o

F

Gas Analysis: 14.0 % CO2 Average Stack Temp., Ts: 132.5 o

F

8.0 % O2 Average √∆p: 0.517 "H2O

0.0 % CO Condensate Volume, Vlc: 110.7 ml

78.0 % N2 Meter Box Y: 1.001 dimensionless

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

Data Calculated from Source Measurements:

Vw(std) = 4.714E-02 x Vlc 5.218 scf

Vm(std) = 17.647 x Vm x Y x (Pb + (∆H / 13.6)) / (Tm +460) 38.486 dscf

Bws = Vw(std) / (Vm(std) + Vw(std)) 0.119 %

FDA = 1.0 - Bws 0.881 %

Md = (0.44 x %CO2) + (0.32 x %O2) + (0.28 x (%N2 + % CO)) 30.56 lb./lb. mole

Ms = (Md x FDA) + (18.0 x Bws) 29.06 lb./lb. mole

vs = 85.49 x Cp x (√∆p) x (√(Ts + 460) / (Ms x Ps)) 30.78 ft/second

Qs = vs x As x 60 1205845.8 acf/minute

Qs(std) = Qs x FDA x (528 / (Ts + 460)) x (Ps / 29.92)) 939879.4 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) 99.2 %

Data from Laboratory Analysis:

Total Particulate Weight From Laboratory Analysis: 0.017100 grams

Calculated Concentration and Emission Rate Data:

cs = (15.432 x grams) / Vm(std) 0.007 grains/dscf

grains/acf = cs x 17.647 x Ps x (FDA / (Ts + 460) 0.005 grains/acf

C = cs / 7000 9.795E-07 lbs/dscf

EM = C x Qs(std) x 60 55.2 lbs/hr

ER = C x Fd x (20.9 /(20.9 - %O2) 0.01552 lbs/MMBtu
Environmental Services

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: CS003 - Common Stack 3

Unit Under Test: Boiler # 3

Operating Conditions: Soot Blowing

Run Number: 2s

Date: 02/25/05

Sample Time, θ: 60 minutes Nozzle Diameter, Dn: 0.287 inches

Barometric Pressure, Pb: 29.69 "Hg Nozzle Area, An: 0.000449 ft2

Stack Pressure, Ps: 29.65 "Hg Average Orifice Meter, ∆H: 1.355 "H2O

Effective Stack Area, As: 652.948 ft2 Sample Volume, Vm: 39.690 ft3

Pitot Coefficient, Cp: 0.84 dimensionless Average Meter Temp., Tm: 85.8 o

F

Gas Analysis: 14.0 % CO2 Average Stack Temp., Ts: 132.3 o

F

8.0 % O2 Average √∆p: 0.510 "H2O

0.0 % CO Condensate Volume, Vlc: 109.8 ml

78.0 % N2 Meter Box Y: 1.001 dimensionless

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

Data Calculated from Source Measurements:

Vw(std) = 4.714E-02 x Vlc 5.176 scf

Vm(std) = 17.647 x Vm x Y x (Pb + (∆H / 13.6)) / (Tm +460) 38.267 dscf

Bws = Vw(std) / (Vm(std) + Vw(std)) 0.119 %

FDA = 1.0 - Bws 0.881 %

Md = (0.44 x %CO2) + (0.32 x %O2) + (0.28 x (%N2 + % CO)) 30.56 lb./lb. mole

Ms = (Md x FDA) + (18.0 x Bws) 29.06 lb./lb. mole

vs = 85.49 x Cp x (√∆p) x (√(Ts + 460) / (Ms x Ps)) 30.35 ft/second

Qs = vs x As x 60 1188859.2 acf/minute

Qs(std) = Qs x FDA x (528 / (Ts + 460)) x (Ps / 29.92)) 925152.9 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) 100.2 %

Data from Laboratory Analysis:

Total Particulate Weight From Laboratory Analysis: 0.019700 grams

Calculated Concentration and Emission Rate Data:

cs = (15.432 x grams) / Vm(std) 0.008 grains/dscf

grains/acf = cs x 17.647 x Ps x (FDA / (Ts + 460) 0.006 grains/acf

C = cs / 7000 1.135E-06 lbs/dscf

EM = C x Qs(std) x 60 63.0 lbs/hr

ER = C x Fd x (20.9 /(20.9 - %O2) 0.01798 lbs/MMBtu
Environmental Services

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: CS003 - Common Stack 3

Unit Under Test: Boiler # 3

Operating Conditions: Soot Blowing

Run Number: 3s

Date: 02/25/05

Sample Time, θ: 60 minutes Nozzle Diameter, Dn: 0.287 inches

Barometric Pressure, Pb: 29.64 "Hg Nozzle Area, An: 0.000449 ft2

Stack Pressure, Ps: 29.61 "Hg Average Orifice Meter, ∆H: 1.349 "H2O

Effective Stack Area, As: 652.948 ft2 Sample Volume, Vm: 39.650 ft3

Pitot Coefficient, Cp: 0.84 dimensionless Average Meter Temp., Tm: 86.0 o

F

Gas Analysis: 13.0 % CO2 Average Stack Temp., Ts: 132.8 o

F

5.0 % O2 Average √∆p: 0.509 "H2O

0.0 % CO Condensate Volume, Vlc: 125.4 ml

82.0 % N2 Meter Box Y: 1.001 dimensionless

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

Data Calculated from Source Measurements:

Vw(std) = 4.714E-02 x Vlc 5.911 scf

Vm(std) = 17.647 x Vm x Y x (Pb + (∆H / 13.6)) / (Tm +460) 38.111 dscf

Bws = Vw(std) / (Vm(std) + Vw(std)) 0.134 %

FDA = 1.0 - Bws 0.866 %

Md = (0.44 x %CO2) + (0.32 x %O2) + (0.28 x (%N2 + % CO)) 30.28 lb./lb. mole

Ms = (Md x FDA) + (18.0 x Bws) 28.63 lb./lb. mole

vs = 85.49 x Cp x (√∆p) x (√(Ts + 460) / (Ms x Ps)) 30.55 ft/second

Qs = vs x As x 60 1196891.6 acf/minute

Qs(std) = Qs x FDA x (528 / (Ts + 460)) x (Ps / 29.92)) 913440.6 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) 101.1 %

Data from Laboratory Analysis:

Total Particulate Weight From Laboratory Analysis: 0.017800 grams

Calculated Concentration and Emission Rate Data:

cs = (15.432 x grams) / Vm(std) 0.007 grains/dscf

grains/acf = cs x 17.647 x Ps x (FDA / (Ts + 460) 0.006 grains/acf

C = cs / 7000 1.030E-06 lbs/dscf

EM = C x Qs(std) x 60 56.4 lbs/hr

ER = C x Fd x (20.9 /(20.9 - %O2) 0.01324 lbs/MMBtu
Environmental Services

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: CS003 - Common Stack 3

Unit Under Test: Boiler # 3

Operating Conditions: Non-Soot Blowing

Run Number: 1

Date: 02/25/05

Sample Time, θ: 60 minutes Nozzle Diameter, Dn: 0.287 inches

Barometric Pressure, Pb: 29.75 "Hg Nozzle Area, An: 0.000449 ft2

Stack Pressure, Ps: 29.72 "Hg Average Orifice Meter, ∆H: 1.297 "H2O

Effective Stack Area, As: 652.948 ft2 Sample Volume, Vm: 38.700 ft3

Pitot Coefficient, Cp: 0.84 dimensionless Average Meter Temp., Tm: 89.4 o

F

Gas Analysis: 14.0 % CO2 Average Stack Temp., Ts: 132.1 o

F

8.0 % O2 Average √∆p: 0.497 "H2O

0.0 % CO Condensate Volume, Vlc: 109.1 ml

78.0 % N2 Meter Box Y: 1.001 dimensionless

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

Data Calculated from Source Measurements:

Vw(std) = 4.714E-02 x Vlc 5.143 scf

Vm(std) = 17.647 x Vm x Y x (Pb + (∆H / 13.6)) / (Tm +460) 37.136 dscf

Bws = Vw(std) / (Vm(std) + Vw(std)) 0.122 %

FDA = 1.0 - Bws 0.878 %

Md = (0.44 x %CO2) + (0.32 x %O2) + (0.28 x (%N2 + % CO)) 30.56 lb./lb. mole

Ms = (Md x FDA) + (18.0 x Bws) 29.03 lb./lb. mole

vs = 85.49 x Cp x (√∆p) x (√(Ts + 460) / (Ms x Ps)) 29.58 ft/second

Qs = vs x As x 60 1158800.3 acf/minute

Qs(std) = Qs x FDA x (528 / (Ts + 460)) x (Ps / 29.92)) 901560.9 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) 99.8 %

Data from Laboratory Analysis:

Total Particulate Weight From Laboratory Analysis: 0.015000 grams

Calculated Concentration and Emission Rate Data:

cs = (15.432 x grams) / Vm(std) 0.006 grains/dscf

grains/acf = cs x 17.647 x Ps x (FDA / (Ts + 460) 0.005 grains/acf

C = cs / 7000 8.905E-07 lbs/dscf

EM = C x Qs(std) x 60 48.2 lbs/hr

ER = C x Fd x (20.9 /(20.9 - %O2) 0.01411 lbs/MMBtu
Environmental Services

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: CS003 - Common Stack 3

Unit Under Test: Boiler # 3

Operating Conditions: Non-Soot Blowing

Run Number: 2

Date: 02/25/05

Sample Time, θ: 60 minutes Nozzle Diameter, Dn: 0.287 inches

Barometric Pressure, Pb: 29.72 "Hg Nozzle Area, An: 0.000449 ft2

Stack Pressure, Ps: 29.69 "Hg Average Orifice Meter, ∆H: 1.266 "H2O

Effective Stack Area, As: 652.948 ft2 Sample Volume, Vm: 38.271 ft3

Pitot Coefficient, Cp: 0.84 dimensionless Average Meter Temp., Tm: 90.0 o

F

Gas Analysis: 14.0 % CO2 Average Stack Temp., Ts: 131.7 o

F

8.0 % O2 Average √∆p: 0.490 "H2O

0.0 % CO Condensate Volume, Vlc: 107.6 ml

78.0 % N2 Meter Box Y: 1.001 dimensionless

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

Data Calculated from Source Measurements:

Vw(std) = 4.714E-02 x Vlc 5.072 scf

Vm(std) = 17.647 x Vm x Y x (Pb + (∆H / 13.6)) / (Tm +460) 36.643 dscf

Bws = Vw(std) / (Vm(std) + Vw(std)) 0.122 %

FDA = 1.0 - Bws 0.878 %

Md = (0.44 x %CO2) + (0.32 x %O2) + (0.28 x (%N2 + % CO)) 30.56 lb./lb. mole

Ms = (Md x FDA) + (18.0 x Bws) 29.03 lb./lb. mole

vs = 85.49 x Cp x (√∆p) x (√(Ts + 460) / (Ms x Ps)) 29.17 ft/second

Qs = vs x As x 60 1142896.5 acf/minute

Qs(std) = Qs x FDA x (528 / (Ts + 460)) x (Ps / 29.92)) 889030.0 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) 99.8 %

Data from Laboratory Analysis:

Total Particulate Weight From Laboratory Analysis: 0.017500 grams

Calculated Concentration and Emission Rate Data:

cs = (15.432 x grams) / Vm(std) 0.007 grains/dscf

grains/acf = cs x 17.647 x Ps x (FDA / (Ts + 460) 0.006 grains/acf

C = cs / 7000 1.053E-06 lbs/dscf

EM = C x Qs(std) x 60 56.2 lbs/hr

ER = C x Fd x (20.9 /(20.9 - %O2) 0.01668 lbs/MMBtu
Environmental Services

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: CS003 - Common Stack 3

Unit Under Test: Boiler # 3

Operating Conditions: Non-Soot Blowing

Run Number: 3

Date: 02/25/05

Sample Time, θ: 60 minutes Nozzle Diameter, Dn: 0.287 inches

Barometric Pressure, Pb: 29.75 "Hg Nozzle Area, An: 0.000449 ft2

Stack Pressure, Ps: 29.72 "Hg Average Orifice Meter, ∆H: 1.334 "H2O

Effective Stack Area, As: 652.948 ft2 Sample Volume, Vm: 39.236 ft3

Pitot Coefficient, Cp: 0.84 dimensionless Average Meter Temp., Tm: 85.0 o

F

Gas Analysis: 14.0 % CO2 Average Stack Temp., Ts: 131.2 o

F

8.0 % O2 Average √∆p: 0.506 "H2O

0.0 % CO Condensate Volume, Vlc: 123.2 ml

78.0 % N2 Meter Box Y: 1.001 dimensionless

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

Data Calculated from Source Measurements:

Vw(std) = 4.714E-02 x Vlc 5.808 scf

Vm(std) = 17.647 x Vm x Y x (Pb + (∆H / 13.6)) / (Tm +460) 37.961 dscf

Bws = Vw(std) / (Vm(std) + Vw(std)) 0.133 %

FDA = 1.0 - Bws 0.867 %

Md = (0.44 x %CO2) + (0.32 x %O2) + (0.28 x (%N2 + % CO)) 30.56 lb./lb. mole

Ms = (Md x FDA) + (18.0 x Bws) 28.89 lb./lb. mole

vs = 85.49 x Cp x (√∆p) x (√(Ts + 460) / (Ms x Ps)) 30.16 ft/second

Qs = vs x As x 60 1181548.1 acf/minute

Qs(std) = Qs x FDA x (528 / (Ts + 460)) x (Ps / 29.92)) 909108.6 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) 101.1 %

Data from Laboratory Analysis:

Total Particulate Weight From Laboratory Analysis: 0.017100 grams

Calculated Concentration and Emission Rate Data:

cs = (15.432 x grams) / Vm(std) 0.0070 grains/dscf

grains/acf = cs x 17.647 x Ps x (FDA / (Ts + 460) 0.0053 grains/acf

C = cs / 7000 9.931E-07 lbs/dscf

EM = C x Qs(std) x 60 54.2 lbs/hr

ER = C x Fd x (20.9 /(20.9 - %O2) 0.01574 lbs/MMBtu
APPENDIX B 

DAILY SULFUR DIOXIDE DATA SUMMARY 
SO2 Data Big Bend 3

Big Bend 3 SO2 Compliance 

Averages- 12.6145 113.6695

Record# DATE TIME CO2_S32 SO2_S34

1 02/25/2005 7:34 12.69 116.1

2 02/25/2005 73500 12.69 112

3 02/25/2005 73600 12.59 100.4

4 02/25/2005 73700 12.64 90.8

5 02/25/2005 73800 12.67 93.3

6 02/25/2005 73900 12.69 97.4

7 02/25/2005 74000 12.64 102.5

8 02/25/2005 74100 12.59 107.4

9 02/25/2005 74200 12.69 108.4

10 02/25/2005 74300 12.74 109

11 02/25/2005 74400 12.72 115.9

12 02/25/2005 74500 12.69 113.8

13 02/25/2005 74600 12.72 108.8

14 02/25/2005 74700 12.7 104.7

15 02/25/2005 74800 12.73 108.8

16 02/25/2005 74900 12.7 114.6

17 02/25/2005 75000 12.67 112.6

18 02/25/2005 75100 12.62 112.2

19 02/25/2005 75200 12.65 119.3

20 02/25/2005 75300 12.59 121.6

21 02/25/2005 75400 12.63 123

22 02/25/2005 75500 12.7 127.6

23 02/25/2005 75600 12.66 126.7

24 02/25/2005 75700 12.66 115.2

25 02/25/2005 75800 12.68 109.5

26 02/25/2005 75900 12.67 103.1

27 02/25/2005 80000 12.66 101.2

28 02/25/2005 80100 12.63 106.6

29 02/25/2005 80200 12.63 108.9

30 02/25/2005 80300 12.62 110

31 02/25/2005 80400 12.63 105.8

32 02/25/2005 80500 12.67 108.9

33 02/25/2005 80600 12.62 111.5

34 02/25/2005 80700 12.55 114.3

35 02/25/2005 80800 12.61 111.2

36 02/25/2005 80900 12.64 109.3

37 02/25/2005 81000 12.59 113.8

38 02/25/2005 81100 12.66 119.2

1 of 13
SO2 Data Big Bend 3

Big Bend 3 SO2 Compliance 

Record# DATE TIME CO2_S32 SO2_S34

39 02/25/2005 81200 12.61 120.9

40 02/25/2005 81300 12.56 118.9

41 02/25/2005 81400 12.69 120.5

42 02/25/2005 81500 12.67 121

43 02/25/2005 81600 12.65 118.6

44 02/25/2005 81700 12.64 111.7

45 02/25/2005 81800 12.6 102.8

46 02/25/2005 81900 12.55 99

47 02/25/2005 82000 12.59 100.5

48 02/25/2005 82100 12.61 105.7

49 02/25/2005 82200 12.65 105.4

50 02/25/2005 82300 12.62 100.7

51 02/25/2005 82400 12.62 101.9

52 02/25/2005 82500 12.56 106.2

53 02/25/2005 82600 12.59 112.9

54 02/25/2005 82700 12.57 110.3

55 02/25/2005 82800 12.55 111.3

56 02/25/2005 82900 12.64 121

57 02/25/2005 83000 12.61 121.9

58 02/25/2005 83100 12.59 111.4

59 02/25/2005 83200 12.62 106.4

60 02/25/2005 83300 12.65 112.9

61 02/25/2005 83400 12.66 115.8

62 02/25/2005 83500 12.67 112

63 02/25/2005 83600 12.63 111.8

64 02/25/2005 83700 12.65 117.1

65 02/25/2005 83800 12.63 122.3

66 02/25/2005 83900 12.62 120.7

67 02/25/2005 84000 12.62 119.3

68 02/25/2005 84100 12.55 121.6

69 02/25/2005 84200 12.53 125.2

70 02/25/2005 84300 12.57 121.5

71 02/25/2005 84400 12.56 108.1

72 02/25/2005 84500 12.62 103.9

73 02/25/2005 84600 12.58 103.8

74 02/25/2005 84700 12.59 100.6

75 02/25/2005 84800 12.58 98.4

76 02/25/2005 84900 12.64 98.4

77 02/25/2005 85000 12.61 98.7

2 of 13
SO2 Data Big Bend 3

Big Bend 3 SO2 Compliance 

Record# DATE TIME CO2_S32 SO2_S34

78 02/25/2005 85100 12.55 91.4

79 02/25/2005 85200 12.61 92.1

80 02/25/2005 85300 12.64 97.4

81 02/25/2005 85400 12.59 99.4

82 02/25/2005 85500 12.65 102

83 02/25/2005 85600 12.62 99.2

84 02/25/2005 85700 12.61 103.1

85 02/25/2005 85800 12.67 108.1

86 02/25/2005 85900 12.72 115.8

87 02/25/2005 90000 12.69 106.5

88 02/25/2005 90100 12.74 92.8

89 02/25/2005 90200 12.75 86.5

90 02/25/2005 90300 12.72 91.6

91 02/25/2005 90400 12.69 96.9

92 02/25/2005 90500 12.71 99.6

93 02/25/2005 90600 12.69 97.8

94 02/25/2005 90700 12.61 97.3

95 02/25/2005 90800 12.66 102.7

96 02/25/2005 90900 12.71 104.5

97 02/25/2005 91000 12.69 108.1

98 02/25/2005 91100 12.62 111.1

99 02/25/2005 91200 12.7 105.2

100 02/25/2005 91300 12.67 101.3

101 02/25/2005 91400 12.67 109.1

102 02/25/2005 91500 12.69 114.1

103 02/25/2005 91600 12.68 132.7

104 02/25/2005 91700 12.64 165.5

105 02/25/2005 91800 12.68 170.4

106 02/25/2005 91900 12.67 168.7

107 02/25/2005 92000 12.68 165.6

108 02/25/2005 92100 12.71 157.2

109 02/25/2005 92200 12.73 136.3

110 02/25/2005 92300 12.72 138.5

111 02/25/2005 92400 12.74 172.2

112 02/25/2005 92500 12.65 201.9

113 02/25/2005 92600 12.6 209

114 02/25/2005 92700 12.64 204.9

115 02/25/2005 92800 12.65 205.5

116 02/25/2005 92900 12.8 212.2

3 of 13
SO2 Data Big Bend 3

Big Bend 3 SO2 Compliance 

Record# DATE TIME CO2_S32 SO2_S34

117 02/25/2005 93000 12.9 215

118 02/25/2005 93100 12.79 200.2

119 02/25/2005 93200 12.83 189.3

120 02/25/2005 93300 12.89 181.6

121 02/25/2005 93400 12.86 168

122 02/25/2005 93500 12.81 167

123 02/25/2005 93600 12.83 163.4

124 02/25/2005 93700 12.85 160.6

125 02/25/2005 93800 12.89 167.4

126 02/25/2005 93900 12.91 167.2

127 02/25/2005 94000 12.9 154

128 02/25/2005 94100 12.85 138.2

129 02/25/2005 94200 12.82 133.3

130 02/25/2005 94300 12.86 134.3

131 02/25/2005 94400 12.87 127.8

132 02/25/2005 94500 12.88 126.3

133 02/25/2005 94600 12.86 127.1

134 02/25/2005 94700 12.81 132.3

135 02/25/2005 94800 12.79 130.1

136 02/25/2005 94900 12.74 125.8

137 02/25/2005 95000 12.76 129.6

138 02/25/2005 95100 12.82 136

139 02/25/2005 95200 12.8 129.9

140 02/25/2005 95300 12.79 124.1

141 02/25/2005 95400 12.85 132.1

142 02/25/2005 95500 12.88 140.4

143 02/25/2005 95600 12.82 137.9

144 02/25/2005 95700 12.8 125.4

145 02/25/2005 95800 12.82 122.4

146 02/25/2005 95900 12.82 125.2

147 02/25/2005 100000 12.86 119.9

148 02/25/2005 100100 12.85 111

153 02/25/2005 100600 12.44 116.9

154 02/25/2005 100700 12.62 111.2

155 02/25/2005 100800 12.74 111.9

10:02 through 10:05 removed from averaging period due to probe blowback.

4 of 13
SO2 Data Big Bend 3

Big Bend 3 SO2 Compliance 

Record# DATE TIME CO2_S32 SO2_S34

156 02/25/2005 100900 12.73 112.6

157 02/25/2005 101000 12.73 113

158 02/25/2005 101100 12.74 116.7

159 02/25/2005 101200 12.67 117.9

160 02/25/2005 101300 12.7 112.6

161 02/25/2005 101400 12.8 115.7

162 02/25/2005 101500 12.73 115.8

163 02/25/2005 101600 12.74 120

164 02/25/2005 101700 12.79 117.3

165 02/25/2005 101800 12.73 116.2

166 02/25/2005 101900 12.79 125.2

167 02/25/2005 102000 12.83 123.2

168 02/25/2005 102100 12.72 123.5

169 02/25/2005 102200 12.72 128.2

170 02/25/2005 102300 12.78 118.7

171 02/25/2005 102400 12.84 116.7

172 02/25/2005 102500 12.84 111.5

173 02/25/2005 102600 12.82 105.2

174 02/25/2005 102700 12.8 103.1

175 02/25/2005 102800 12.81 106.7

176 02/25/2005 102900 12.78 111.4

177 02/25/2005 103000 12.89 113

178 02/25/2005 103100 12.8 106.9

179 02/25/2005 103200 12.81 108.1

180 02/25/2005 103300 12.82 112

181 02/25/2005 103400 12.8 114.2

182 02/25/2005 103500 12.73 113.7

183 02/25/2005 103600 12.73 114.7

184 02/25/2005 103700 12.74 120.2

185 02/25/2005 103800 12.7 117.7

186 02/25/2005 103900 12.74 118.2

187 02/25/2005 104000 12.75 117.3

188 02/25/2005 104100 12.77 111.4

189 02/25/2005 104200 12.75 109.2

190 02/25/2005 104300 12.79 113.1

191 02/25/2005 104400 12.74 112.8

192 02/25/2005 104500 12.75 118.2

193 02/25/2005 104600 12.77 115.4

194 02/25/2005 104700 12.75 114.3

5 of 13
SO2 Data Big Bend 3

Big Bend 3 SO2 Compliance 

Record# DATE TIME CO2_S32 SO2_S34

195 02/25/2005 104800 12.72 116.6

196 02/25/2005 104900 12.76 122.3

197 02/25/2005 105000 12.79 125

198 02/25/2005 105100 12.79 116.2

199 02/25/2005 105200 12.79 106

200 02/25/2005 105300 12.78 98.6

201 02/25/2005 105400 12.8 97.4

202 02/25/2005 105500 12.73 96.5

203 02/25/2005 105600 12.77 96.4

204 02/25/2005 105700 12.77 95.8

205 02/25/2005 105800 12.73 96.2

206 02/25/2005 105900 12.72 97.1

207 02/25/2005 110000 12.74 96

208 02/25/2005 110100 12.74 95.3

209 02/25/2005 110200 12.78 98.5

210 02/25/2005 110300 12.8 105

211 02/25/2005 110400 12.8 104

212 02/25/2005 110500 12.77 101.7

213 02/25/2005 110600 12.81 105.1

214 02/25/2005 110700 12.82 112.8

215 02/25/2005 110800 12.88 114.5

216 02/25/2005 110900 12.84 109

217 02/25/2005 111000 12.74 108.1

218 02/25/2005 111100 12.7 112.4

219 02/25/2005 111200 12.7 113.8

220 02/25/2005 111300 12.71 112.2

221 02/25/2005 111400 12.82 111

222 02/25/2005 111500 12.74 102.2

223 02/25/2005 111600 12.7 95

224 02/25/2005 111700 12.74 93.2

225 02/25/2005 111800 12.75 96.8

226 02/25/2005 111900 12.7 96.6

227 02/25/2005 112000 12.7 97.9

228 02/25/2005 112100 12.7 100.6

229 02/25/2005 112200 12.74 103.1

230 02/25/2005 112300 12.73 110.6

231 02/25/2005 112400 12.73 110.9

232 02/25/2005 112500 12.67 105.8

233 02/25/2005 112600 12.74 102.6

6 of 13
SO2 Data Big Bend 3

Big Bend 3 SO2 Compliance 

Record# DATE TIME CO2_S32 SO2_S34

234 02/25/2005 112700 12.76 102.4

235 02/25/2005 112800 12.69 107.5

236 02/25/2005 112900 12.75 104.3

237 02/25/2005 113000 12.64 101.8

238 02/25/2005 113100 12.6 103

239 02/25/2005 113200 12.62 107.6

240 02/25/2005 113300 12.7 103.8

241 02/25/2005 113400 12.74 102.5

242 02/25/2005 113500 12.65 105.7

243 02/25/2005 113600 12.7 112.3

244 02/25/2005 113700 12.7 116.6

245 02/25/2005 113800 12.74 117

246 02/25/2005 113900 12.74 112.9

247 02/25/2005 114000 12.77 106.4

248 02/25/2005 114100 12.65 99.6

249 02/25/2005 114200 12.65 93.4

250 02/25/2005 114300 12.75 96.2

251 02/25/2005 114400 12.73 97.3

252 02/25/2005 114500 12.62 100.2

253 02/25/2005 114600 12.66 99.5

254 02/25/2005 114700 12.61 96.8

255 02/25/2005 114800 12.69 100.8

256 02/25/2005 114900 12.63 107.5

257 02/25/2005 115000 12.6 108.6

258 02/25/2005 115100 12.56 106.5

259 02/25/2005 115200 12.59 107.8

260 02/25/2005 115300 12.6 110.6

261 02/25/2005 115400 12.65 116.3

262 02/25/2005 115500 12.65 108.5

263 02/25/2005 115600 12.62 108.6

264 02/25/2005 115700 12.57 109.1

265 02/25/2005 115800 12.61 110.2

266 02/25/2005 115900 12.64 115.6

267 02/25/2005 120000 12.66 109.2

268 02/25/2005 120100 12.63 101.3

269 02/25/2005 120200 12.67 101.1

270 02/25/2005 120300 12.69 101.8

271 02/25/2005 120400 12.67 97.5

272 02/25/2005 120500 12.67 101.6

7 of 13
SO2 Data Big Bend 3

Big Bend 3 SO2 Compliance 

Record# DATE TIME CO2_S32 SO2_S34

273 02/25/2005 120600 12.61 106.2

274 02/25/2005 120700 12.58 107.7

275 02/25/2005 120800 12.57 103.6

276 02/25/2005 120900 12.6 107.3

277 02/25/2005 121000 12.65 111.3

278 02/25/2005 121100 12.66 110.5

279 02/25/2005 121200 12.67 104.6

280 02/25/2005 121300 12.6 102.8

281 02/25/2005 121400 12.6 101.9

282 02/25/2005 121500 12.59 107.1

283 02/25/2005 121600 12.6 113

284 02/25/2005 121700 12.64 114.4

285 02/25/2005 121800 12.58 110.9

286 02/25/2005 121900 12.53 112.1

287 02/25/2005 122000 12.58 117.9

288 02/25/2005 122100 12.63 115

289 02/25/2005 122200 12.65 103.7

290 02/25/2005 122300 12.61 96.6

291 02/25/2005 122400 12.61 96.6

292 02/25/2005 122500 12.67 99.4

293 02/25/2005 122600 12.61 99.3

294 02/25/2005 122700 12.7 99.9

295 02/25/2005 122800 12.66 99.8

296 02/25/2005 122900 12.67 96.7

297 02/25/2005 123000 12.7 98.1

298 02/25/2005 123100 12.66 100.2

299 02/25/2005 123200 12.61 105.7

300 02/25/2005 123300 12.62 104.1

301 02/25/2005 123400 12.57 103.5

302 02/25/2005 123500 12.59 105

303 02/25/2005 123600 12.6 108

304 02/25/2005 123700 12.62 110.5

305 02/25/2005 123800 12.63 108.6

306 02/25/2005 123900 12.63 107.9

307 02/25/2005 124000 12.66 116.3

308 02/25/2005 124100 12.65 121.2

309 02/25/2005 124200 12.63 116.1

310 02/25/2005 124300 12.62 114.7

311 02/25/2005 124400 12.63 113.8

8 of 13
SO2 Data Big Bend 3

Big Bend 3 SO2 Compliance 

Record# DATE TIME CO2_S32 SO2_S34

312 02/25/2005 124500 12.61 112.4

313 02/25/2005 124600 12.54 116.5

314 02/25/2005 124700 12.6 121

315 02/25/2005 124800 12.67 117.8

316 02/25/2005 124900 12.53 113

317 02/25/2005 125000 12.52 116.2

318 02/25/2005 125100 12.55 115.5

319 02/25/2005 125200 12.65 115.4

320 02/25/2005 125300 12.67 110.6

321 02/25/2005 125400 12.62 102.2

322 02/25/2005 125500 12.56 100.6

323 02/25/2005 125600 12.58 102.7

324 02/25/2005 125700 12.59 109.7

325 02/25/2005 125800 12.61 109.5

326 02/25/2005 125900 12.59 101.4

327 02/25/2005 130000 12.58 98.8

328 02/25/2005 130100 12.56 102.4

329 02/25/2005 130200 12.6 108

330 02/25/2005 130300 12.59 105.6

331 02/25/2005 130400 12.64 100.8

332 02/25/2005 130500 12.66 102.6

333 02/25/2005 130600 12.66 109.4

334 02/25/2005 130700 12.62 111.5

335 02/25/2005 130800 12.62 110

336 02/25/2005 130900 12.63 109.8

337 02/25/2005 131000 12.66 114.5

338 02/25/2005 131100 12.63 118

339 02/25/2005 131200 12.6 116.4

340 02/25/2005 131300 12.56 123

341 02/25/2005 131400 12.6 123.7

342 02/25/2005 131500 12.61 120.5

343 02/25/2005 131600 12.59 121.1

344 02/25/2005 131700 12.6 125.2

345 02/25/2005 131800 12.59 118.5

346 02/25/2005 131900 12.58 105

347 02/25/2005 132000 12.59 100.8

348 02/25/2005 132100 12.64 101.6

349 02/25/2005 132200 12.61 102.3

350 02/25/2005 132300 12.59 103.1

9 of 13
SO2 Data Big Bend 3

Big Bend 3 SO2 Compliance 

Record# DATE TIME CO2_S32 SO2_S34

351 02/25/2005 132400 12.63 104.7

352 02/25/2005 132500 12.59 108

353 02/25/2005 132600 12.55 105.3

354 02/25/2005 132700 12.58 106.7

355 02/25/2005 132800 12.61 109.7

356 02/25/2005 132900 12.58 114.9

357 02/25/2005 133000 12.59 118.1

358 02/25/2005 133100 12.61 115

359 02/25/2005 133200 12.61 116.1

360 02/25/2005 133300 12.6 113.5

361 02/25/2005 133400 12.61 108.9

362 02/25/2005 133500 12.6 106.5

363 02/25/2005 133600 12.59 110

364 02/25/2005 133700 12.57 111.8

365 02/25/2005 133800 12.55 111.6

366 02/25/2005 133900 12.56 120.6

367 02/25/2005 134000 12.66 122.1

368 02/25/2005 134100 12.64 117.4

369 02/25/2005 134200 12.5 115.4

370 02/25/2005 134300 12.51 116.7

371 02/25/2005 134400 12.54 108.9

372 02/25/2005 134500 12.62 104.8

373 02/25/2005 134600 12.57 102.3

374 02/25/2005 134700 12.54 107.7

375 02/25/2005 134800 12.5 107.5

376 02/25/2005 134900 12.55 111.7

377 02/25/2005 135000 12.65 111.6

378 02/25/2005 135100 12.59 109.4

379 02/25/2005 135200 12.63 109.8

380 02/25/2005 135300 12.64 109.3

381 02/25/2005 135400 12.56 106.4

382 02/25/2005 135500 12.55 112.6

383 02/25/2005 135600 12.55 114.8

384 02/25/2005 135700 12.49 111.6

385 02/25/2005 135800 12.52 114.3

386 02/25/2005 135900 12.6 117.5

387 02/25/2005 140000 12.47 124.2

388 02/25/2005 140100 12.4 122.6

389 02/25/2005 140200 12.44 118.2

10 of 13
SO2 Data Big Bend 3

Big Bend 3 SO2 Compliance 

Record# DATE TIME CO2_S32 SO2_S34

390 02/25/2005 140300 12.4 121.5

391 02/25/2005 140400 12.41 128.4

392 02/25/2005 140500 12.45 122.9

393 02/25/2005 140600 12.39 114.4

394 02/25/2005 140700 12.43 120.8

395 02/25/2005 140800 12.5 123.1

396 02/25/2005 140900 12.5 125

397 02/25/2005 141000 12.4 120.8

398 02/25/2005 141100 12.46 120.5

399 02/25/2005 141200 12.48 121.8

400 02/25/2005 141300 12.52 120

401 02/25/2005 141400 12.54 118.3

402 02/25/2005 141500 12.57 120.9

403 02/25/2005 141600 12.46 116.7

404 02/25/2005 141700 12.44 112.2

405 02/25/2005 141800 12.55 106.4

406 02/25/2005 141900 12.53 103.3

407 02/25/2005 142000 12.52 105.7

408 02/25/2005 142100 12.42 110.3

409 02/25/2005 142200 12.36 107.3

410 02/25/2005 142300 12.49 108

411 02/25/2005 142400 12.48 114.4

412 02/25/2005 142500 12.48 116.6

413 02/25/2005 142600 12.43 111.4

414 02/25/2005 142700 12.48 105.3

415 02/25/2005 142800 12.52 105.7

416 02/25/2005 142900 12.47 109.4

417 02/25/2005 143000 12.45 108.9

418 02/25/2005 143100 12.46 102

419 02/25/2005 143200 12.43 105.9

420 02/25/2005 143300 12.35 106.5

421 02/25/2005 143400 12.33 107.1

422 02/25/2005 143500 12.43 106.5

423 02/25/2005 143600 12.43 109.5

424 02/25/2005 143700 12.44 113.7

425 02/25/2005 143800 12.48 119.9

426 02/25/2005 143900 12.52 119.9

427 02/25/2005 144000 12.49 117.3

428 02/25/2005 144100 12.46 122.6

11 of 13
SO2 Data Big Bend 3

Big Bend 3 SO2 Compliance 

Record# DATE TIME CO2_S32 SO2_S34

429 02/25/2005 144200 12.43 118.9

430 02/25/2005 144300 12.48 104.6

431 02/25/2005 144400 12.45 96.5

432 02/25/2005 144500 12.47 93.7

433 02/25/2005 144600 12.48 98.4

434 02/25/2005 144700 12.47 100.3

435 02/25/2005 144800 12.48 103.5

436 02/25/2005 144900 12.44 100.3

437 02/25/2005 145000 12.49 102.7

438 02/25/2005 145100 12.48 106.1

439 02/25/2005 145200 12.45 107.7

440 02/25/2005 145300 12.48 104.3

441 02/25/2005 145400 12.4 105.7

442 02/25/2005 145500 12.39 106.6

443 02/25/2005 145600 12.43 108

444 02/25/2005 145700 12.38 109.8

445 02/25/2005 145800 12.44 115.8

446 02/25/2005 145900 12.44 121.4

447 02/25/2005 150000 12.49 117.8

448 02/25/2005 150100 12.44 115

449 02/25/2005 150200 12.34 112.4

450 02/25/2005 150300 12.39 110.7

451 02/25/2005 150400 12.4 110.1

452 02/25/2005 150500 12.34 114.9

453 02/25/2005 150600 12.37 115.6

454 02/25/2005 150700 12.38 111.4

455 02/25/2005 150800 12.33 109.5

456 02/25/2005 150900 12.36 116.2

457 02/25/2005 151000 12.37 120.7

458 02/25/2005 151100 12.44 121.7

459 02/25/2005 151200 12.43 123.4

460 02/25/2005 151300 12.42 123.5

461 02/25/2005 151400 12.36 120.8

462 02/25/2005 151500 12.31 119.6

463 02/25/2005 151600 12.37 122

464 02/25/2005 151700 12.41 127.4

465 02/25/2005 151800 12.42 127.2

466 02/25/2005 151900 12.37 112

467 02/25/2005 152000 12.36 99.8

12 of 13
SO2 Data Big Bend 3

Big Bend 3 SO2 Compliance 

Record# DATE TIME CO2_S32 SO2_S34

468 02/25/2005 152100 12.48 98.6

469 02/25/2005 152200 12.46 101.5

470 02/25/2005 152300 12.47 105.8

471 02/25/2005 152400 12.41 109.6

472 02/25/2005 152500 12.39 108.7

473 02/25/2005 152600 12.37 105.5

474 02/25/2005 152700 12.4 105.8

475 02/25/2005 152800 12.43 109.8

476 02/25/2005 152900 12.39 109.7

477 02/25/2005 153000 12.4 107.8

478 02/25/2005 153100 12.4 112.1

479 02/25/2005 153200 12.36 115.8

480 02/25/2005 153300 12.34 120

481 02/25/2005 153400 12.39 118.3

482 02/25/2005 153500 12.46 119.5

483 02/25/2005 153600 12.47 120.8

484 02/25/2005 153700 12.4 114.6

485 02/25/2005 153800 12.47 112.6

486 02/25/2005 153900 12.47 115.2

487 02/25/2005 154000 12.39 114.9

488 02/25/2005 154100 12.38 119.1

489 02/25/2005 154200 12.38 118.8

490 02/25/2005 154300 12.41 115.2

491 02/25/2005 154400 12.41 105.5

492 02/25/2005 154500 12.32 96.9

493 02/25/2005 154600 12.32 99.6

494 02/25/2005 154700 12.35 105.3

495 02/25/2005 154800 12.37 104.6

496 02/25/2005 154900 12.42 109.7

497 02/25/2005 155000 12.38 105.9

498 02/25/2005 155100 12.45 101.8

499 02/25/2005 155200 12.46 100.2

500 02/25/2005 155300 12.32 99.5

501 02/25/2005 155400 12.29 96.6

502 02/25/2005 155500 12.36 96.7

503 02/25/2005 155600 12.4 103.2

504 02/25/2005 155700 12.31 103.9

505 02/25/2005 15:58 12.34 101.8

Averages: 12.615 113.669

13 of 13
APPENDIX C 

PARTICULATE LABORATORY ANALYTICAL DATA 
Customer Big Bend Plant Big Bend Unit 3

Method 5-B Stack Test Completion Date 02/25/2005Analyst GAH/SS Sample Number AA76139

ACETONE BEAKER 1st weighing Date 03/02/2005 Time 16:50 % RH 31.0%

2nd weighing Date 03/03/2005 Time 15:18 % RH 38.0%

3rd weighing Date 03/04/2005 Time 10:10 % RH 40.0%

4th weighing Date 03/04/2005 Time 16:30 % RH 38.0%

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

Acetone Container ID Air 19 Air 5 Air R2 Air B2 Air 17 Air AA Air 05

Acetone Rinse Vol.(Va), mls 200.0000 200 200 200 200 200 200

1st Gross Wt., grams 106.4615 101.4518 103.7493 108.4180 105.1044 106.3647 106.8296

2nd Gross Wt., grams 106.4611 101.4508 103.7483 108.4162 105.1031 106.3629 106.8264

3rd Gross Wt., grams 106.4604 101.4506 103.7479 108.4165 105.1026 106.3629 106.8260

4th Gross Wt., grams 106.4603

Avg. Gross Wt., grams 106.46130 101.45070 103.74810 108.41635 105.10285 106.36290 106.82620

Tare Wt., grams 106.46030 101.44605 103.74060 108.40955 105.09725 106.35540 106.82100

Acetone Blank Wt., mg 1.00 1.00 1.00 1.00 1.00 1.00 1.00

Acetone Particulate Wt., mg 3.65 6.50 5.80 4.60 6.50 4.20

Acetone Residue, mg/g 0.0063

Acetone Blank Criteria

 FILTER 1st weighing Date 03/01/2005 Time 16:50 % RH 43.0%

 Date 03/02/2005 Time 11:35 % RH 34.0%

3rd weighing Date 03/02/2005 Time 17:40 % RH 31.0%

4th weighing Date 03/03/2005 Time 15:10 % RH 38.0%

Filter/Thimble ID 202315 202309 202310 202314 202307 202313 202308

1st Gross Wt., grams 0.2651 0.2798 0.2753 0.2787 0.2802 0.2725 0.2828

2nd Gross Wt., grams 0.2650 0.2791 0.2745 0.2778 0.2794 0.2714 0.2821

3rd Gross Wt., grams 0.2651 0.2790 0.2745 0.2781 0.2801 0.2726 0.2828

4th Gross Wt., grams 0.2802 0.2725 0.2829

Avg. Gross Wt., grams 0.26505 0.27905 0.27450 0.27795 0.28015 0.27255 0.28285

Tare Wt., grams 0.26495 0.26770 0.26350 0.26665 0.26765 0.25935 0.26925

Filter Particulate Wt., mg 11.35 11.00 11.30 12.50 13.20 13.60

Difference, milligrams 0.1

Total Sample Particulate Wt., mg 15.00 17.50 17.10 17.10 19.70 17.80

OK to subtract acetone blank

Start Here
APPENDIX D 

BOILER/PRECIPITATOR OPERATIONAL DATA 







APPENDIX E 

FUEL ANALYSIS 

APPENDIX F 

FIELD DATA SHEETS 










APPENDIX G 

SAMPLING EQUIPMENT CALIBRATIONS 
SUMMARY OF EQUIPMENT CALIBRATIONS

EQUIPMENT CAL DATE METHOD RESULTS

CONSOLE (MB 07) USEPA RM 5

INITIAL 10/05/2004 (ORIFICE) 1.001

POST TEST 03/01/2005 0.997

NOZZLE SN19

INITIAL 01/10/2005 CALIPER 0.287

POST TEST 03/01/2005 MEASUREMENTS 0.285

PYROMETER (PY 09) 01/04/2005 ASTM THERMOMETER + 2o

 F

PITOT TUBE (PT 08) 01/19/2005 USEPA RM 2 Cp = 0.84

BAROMETER (BR 02) 03/02/2005 NWS COMPARISON + 0.01" Hg
Environmental Services

Air Services Group

Blue Team

Manufacturer: Thermo Anderson Calibration Date:

Model Number:MST-C1 Barometric Pressure: 30.25 "Hg

Instrument Code Number: ^MB07 Theoretical Critical Vacuum: 14.27 "Hg

LabWorks Sample Number: Calibrated By:

Initial Final Total

∆H Time Volume Volume Volume Inlet Outlet Inlet Outlet

"H2O Minutes ft

3 ft3 ft3

oF oF oF oF

0.62 15 3.577 10.434 6.857 79 81 79 81

1.15 15 93.523 102.765 9.242 83 78 79 81

1.90 15 69.792 81.726 11.934 81 89 87 81

3.65 15 21.691 38.150 16.459 85 96 86 96

Orifice K' Actual

Serial Orifice Vacuum Initial Final Average

Number Coefficient "Hg oF oF oF

48 0.3483 20.0 75 76 75.5

55 0.4660 19.0 77 75 76.0

63 0.5971 17.0 72 72 72.0

73 0.8177 14.0 73 73 73.0

Dry Gas Meter Calibration Calibration

Volume Volume Volume Y ∆Hα

Corrected Corrected Nominal Value QA/QC Value QA/QC

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

6.786 6.830 6.854 1.006 0.006 1.663 -0.044

9.154 9.133 9.174 0.998 -0.003 1.724 0.017

11.749 11.746 11.711 1.000 -0.001 1.709 0.001

16.088 16.071 16.053 0.999 -0.002 1.734 0.026

Averages: 1.001 1.707

Review/Approval: 8-Oct-04

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

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

10/05/2004

CRD

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: 30.1 "Hg

Instrument Code Number: MB07 Theoretical Critical Vacuum: 14.20 "Hg

LabWorks Sample Number: Calibrated By:

Associated Test: Team: BLUE

Initial Final Total

∆H Time Volume Volume Volume Inlet Outlet Inlet Outlet

"H2O Minutes ft3 ft3 ft3

oF oF oF oF

1.10 10 354.350 360.474 6.124 73 77 74 78

1.10 10 360.474 366.612 6.138 74 78 75 78

1.10 10 366.612 372.762 6.150 75 78 75 79

Orifice K' Actual

Serial Orifice Vacuum Initial Final Average

Number Coefficient "Hg oF oF oF

55 0.4660 17.5 74 72 73.0

55 0.4660 17.5 72 72 72.0

55 0.4660 17.5 72 73 72.5

Dry Gas Meter Calibration Calibration

Volume Volume Volume Y ∆Hα

Corrected Corrected Nominal Value QA/QC Value QA/QC

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

6.088 6.076 6.099 0.998 0.000 1.663 0.004

6.094 6.081 6.093 0.998 0.001 1.657 -0.002

6.100 6.078 6.096 0.996 -0.001 1.657 -0.002

Averages: 0.997 1.659

Prior Y: 1.001

% Difference: 0.36%

Review/Approval: Date:

Big Bend 3 compliance

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

Initial Temperatures Final Tempertures

Critical Orifice Readings

USEPA Reference Method 5

Dry Gas Meter Calibration

Critical Orifice Method

Charles Dufeny

03/01/2005

POST - TEST CALIBRATION CHECK

3-Mar-2005

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

Critical Orifice
Environmental Services

Air Services Group

QUARTERLY NOZZLE CALIBRATIONS

Shared Resource

STEEL NOZZLE SET

Calibration Date: 01/10/2005 Responsible Party: Jorge A. Varino

Nozzle Nozzle Diameter, Dn (cm) Maximum Average

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

^SN01 0.300 0.300 0.300 0.000 0.118

^SN04 0.320 0.320 0.320 0.000 0.126

^SN05 0.380 0.380 0.380 0.000 0.150

^SN06 0.500 0.500 0.500 0.000 0.197

^SN09 0.697 0.700 0.700 0.001 0.275

^SN10 0.750 0.755 0.750 0.002 0.296

^SN12 0.985 0.990 0.990 0.002 0.389

^SN15 0.420 0.420 0.420 0.000 0.165

^SN16 0.505 0.505 0.505 0.000 0.199

^SN19 0.725 0.730 0.730 0.002 0.287

^SN22 0.940 0.935 0.940 0.002 0.369

^SN30 0.790 0.800 0.800 0.004 0.314

^SN36 0.480 0.475 0.480 0.002 0.188

^SN37 0.530 0.530 0.530 0.000 0.209

^SN38 0.640 0.640 0.645 0.002 0.253

^SN46 0.485 0.480 0.485 0.002 0.190

^SN47 0.515 0.520 0.515 0.002 0.203

^SN48 0.640 0.645 0.640 0.002 0.253

^SN50 0.790 0.795 0.795 0.002 0.312

^SN58 0.615 0.620 0.615 0.002 0.243

^SN68 0.625 0.630 0.630 0.002 0.247

^SN69 0.945 0.950 0.945 0.002 0.373

^SN70 1.560 1.560 1.560 0.000 0.614

^SN71 1.555 1.560 1.560 0.002 0.614

^SN72 0.955 0.950 0.950 0.002 0.375

^SN73 1.290 1.290 1.285 0.002 0.507

^SN74 1.240 1.245 1.245 0.002 0.490

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: 13-Jan-05
Environmental Services

Air Services Group

POST TEST NOZZLE CALIBRATION 

Shared Resource

Calibration Date: 03/01/2005

Calibration Personnel: Charles Dufeny

Test Designation: Big Bend 3 Compliance

Nozzle Nozzle Diameter, Dn (cm) Maximum Average

Identifier D1 D2 D3 Difference, " Dn, inches

SN19 0.730 0.720 0.720 0.004 0.285

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 0.287

QA/QC Review by: 3-Mar-2005
Pyrometer Calibration

Pyrometer Under Test

Pyrometer Number: ^PY09

Labworks Sample # 0

Calibration Date: 01/04/2005

Calibrator Information

Calibrator Type/Manufacturer: Hart Scientific

Calibrator Serial Number: AOA024

Date of Last Calibration: 07/08/2004

Calibration Personnel (Typed and Signature): JORGE A VARINO

Calibration Data

Calibration Reference Pyrometer

Point Temperature Indication Difference

1 400 399 1

2 212 211 1

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

This data has been reviewed and is certified as meeting all project quality objectives.

Reviewer: Date: 6-Jan-2005
c

PITOT TUBE CALIBRATION

DATA SHEET

Pitot Tube ID # pt08

Calibration Date: 01/19/2005 Operating Quarter: 1

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

Alpha and Beta Angle Determinations Acceptable Limits:

α 1 0.3 degrees Pass Dt 0.48 < Dt > 0.95 cm

α 2 0.5 degrees Pass α < 10 degrees

β 1 0 degrees Pass (α1 measured across top impact openings)

β 2 0.4 degrees Pass (α2 measured across bottom impact openings)

β1 < 5 degrees (alongside top impact openings)

Gamma, Theta, A, Z, and W Determinations β2 < 5 degrees (alongside bottom impact openings)

ψ 1.4 degrees Z < 0.32 cm (Asinψ)

Α 2.375 cm W < 0.08 cm (Asinο)

Ζ 0.058 cm Pass A distance between tips

ο angle of plane on side of pitots

ο 1.8 degrees ψ angle between tips

W 0.075 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 Specifi

Methods", sub-section 3.1.1, Procurement of Apparatus and Supplies.

Comments: REVMOVABLE

Printed Name: Charles Dufeny Date: 01/19/2005

Quality Assurance Review / Approval: 21-Jan-2005

5010 Causeway Blvd., Tampa, FL. 33619
Environmental Services

Air Services Group

BAROMETER CALIBRATION

Red Team

Instrument Number: BR02

Calibration Date: 03/02/2005

Calibration Personnel: Charles Dufeny

Barometer Reading Reference Reading Difference

Time Inches Mercury Inches Mercury "Hg

9:53 30.18 30.20 -0.02

10:53 30.20 30.20 0.00

12:53 30.15 30.16 -0.01

Average Difference: -0.01

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

Current Reference is National Weather Service, Ruskin Florida.

Comments (Note any adjustments):

QA/QC Review by: Date: 4-Mar-2005
APPENDIX H 

CHAIN OF CUSTODY 


APPENDIX I 

TEST PARTICIPANTS 
TEST PARTICIPANTS

AIR SERVICES GROUP 

ENVIRONMENTAL SERVICES

Charles Dufeny Environmental Technician 

Jorge Varino Technician 

Ray McDarby Senior Environmental Technician 

BIG BEND STATION

Karen Zwolak Senior Environmental Consultant