# Results of the March 11-22, 

# 2008 Sulfur Dioxide Engineering Testing on the Pellet Indurating Furnace (EU026) Stacks SV014, SV015, SV016 and SV017 at ArcelorMittal Minorca Mine, Inc. Located in Virginia, Minnesota AQ File Number 257 AQ Facility Per/nit NU111ber 

# 13700062-002 Prepared for ArcelorMittal Min orca Mines, Inc.
March 

# 2009

Prepared by Barr Engineering Company 4700 West 71 h 

# Street Minneapolis, MN 55435-4803 Phone: (952) 

# 832-2600 Fax: (952) 

# 832-2601



# Results of the March 11-22, 

# 2008 Sulfur Dioxide Engineering Testing on the Pellet Indurating Furnace (EU026) Stacks SV014, SV015, SV016 and SV017 at ArcelorMittal Minorca Mine, Inc. Located in Virginia, Minnesota AQ File Number 257 AQ Facility Per/nit NU111ber 

# 13700062-002 Prepared for ArcelorMittal Minorca Mines, Inc.
March 

# 2009

Prepared by Barr Engineering Company 4700 

# West 71h 

# Street Minneapolis, MN 55435-4803 

# Phone: (952) 

# 832-2600 Fax: (952) 

# 832-2601

# Results of the March 11-22, 

# 2008 Sulfur Dioxide Engineering Testing on the Pellet Indurating Furnace (EU026) Stacks SV014, SV015, SV016 and SV017 at ArcelorMittal Minorca Mine, Inc. Located in Virginia, Minnesota AQ File Number 257 AQ Facility Permit Number 13700062-002 Prepared for ArcelorMittal Min orca Mines, Inc. March 2009



# BARR 4700 West 71 h 

# Street Minneapolis, MN 55435-4803 Phone: (952) 

# 832-2600 Fax: (952) 

# 832-2601 

# Results of the March 11-22, 

# 2008 Sulfur Dioxide Engineering Testing on the Pellet Indurating Furnace (EU026) Stacks SV014, SV015, SV016 and SV017 at ArcelorMittal Minorca Mine, Inc. Located in Virginia, Minnesota AQ File Number 257 AQ Facility Permit Number 13700062-002 Prepared for ArcelorMittal Minorca Mines, Inc. March 2009



# BARR 4700 

# West 71h 

# Street Minneapolis, MN 55435-4803 

# Phone: (952) 

# 832-2600 Fax: (952) 

# 832-2601

# Results of the March 11-22, 2008 Sulfur Dioxide Engineering Testing on the Pellet Indurating Furnace (EU026) Stacks SV014, SV015, SV016 and SV017 at ArcelorMittal Minorca Mine, Inc. Located in Virginia, Minnesota Table of Contents
Executive summary 1 Introduction 2 Results 3 Process description 5 Stack testing procedures and methods 6 

# Results of the March 11-22, 2008 Sulfur Dioxide Engineering Testing on the Pellet Indurating Furnace (EU026) Stacks SV014, SV015, SV016 and SV017 at ArcelorMittal Minorca Mine, Inc. Located in Virginia, Minnesota Table of Contents
Executive summary ....................................................................................................................................... 1 Introduction
................................................................................................................................................... 2 Results
........................................................................................................................................................... 3 Process description
........................................................................................................................................ 5 Stack testing procedures and methods
.......................................................................................................... 6

# Table 1

Figure 1 Figure 2 Figure 3 Figure 4 

# List of Tables S02 Test Results Summary



# List of Figures Test Port Locations

- Pellet Indurating Furnace Line 2 (SVO14, SVO15), (EU026) Traverse Point Locations

- Pellet Indurating Furnace Line 2 (SVOI4, SVOI5, (EU026) Test Port Locations

- Pellet Indurating Furnace Line 2 (SVO16, SVO 17), (EU026) Traverse Point Locations

- Pellet Indurating Furnace Line 2 (SVOI6, SVOI7), (EU026)



# List of Appendices Appendix A Appendix B Appendix C Appendix D Appendix E Appendix F Appendix G Appendix H Report Calculations and Nomenclature Field Data Sheets Instrument Output Calibration Data Cylinder Gas Certifications Process Operating Data Stack Test Plan Project Participants and Contact Information

11 

# List of Tables Table 1 S02 Test Results Summary



# List of Figures Figure 1 Test Port Locations

- Pellet Indurating Furnace Line 2 (SVO 14, SVO 15), (EU026) Figure 2 Traverse Point Locations

- Pellet Indurating Furnace Line 2 (SVOI4, SVOI5, (EU026) Figure 3 Test Port Locations

- Pellet Indurating Furnace Line 2 (SVO 16, SVO 17), (EU026) Figure 4 Traverse Point Locations

- Pellet Indurating Furnace Line 2 (SVOI6, SVOI7), (EU026)



# List of Appendices Appendix A Report Calculations and Nomenclature Appendix B Field Data Sheets Appendix C Instrument Output Appendix D Calibration Data Appendix E Cylinder Gas Certifications Appendix F Process Operating Data Appendix G Stack Test Plan Appendix H Project Participants and Contact Information

11

# Executive summa
Barr Engineering performed sulfur dioxide (S02) emissions testing at ArcelorMittal Minorca Mine, Inc. (ArcelorMittal) located in Virginia, Minnesota from March 11 through March 22, 2008. The testing was performed for engineering purposes to collect S02 emissions data during normal taconite processing operations from the induration furnace exhaust stacks (A-D). S02 emissions were measured simultaneously from three of the four indurating furnace waste gas stacks. Data was collected from all four stacks over the testing period. The data was collected during the NO x Relative Variability Index testing project. 

# Executive Summary Table Stack A Stack B Stack C Stack D Combined Data collection period 3/12-14/08 3/12-14/08 3/20-22/08 3/12-14/08 3/17-22/08 3/17-22/08 3/17-20/08 3/17-22/08 Average S02 Emission Rate, 8.9 7.0 5.3 4.6 25.7 lb/hr Fired Pellet Production Rate, LTPH 235.9 (testing period average) Emission Factor, S02 lb/LT Fired Pellet 0.113 (testing period average)

23 69C06003 - I 

# Executive summa
Barr Engineering performed sulfur dioxide (S02) emissions testing at ArcelorMittal Minorca Mine, Inc. (ArcelorMittal) located in Virginia, Minnesota from March 11 through March 22, 2008. The testing was performed for engineering purposes to collect S02 emissions data during normal taconite processing operations from the induration furnace exhaust stacks (A-D). S02 emissions were measured simultaneously from three of the four indurating furnace waste gas stacks. Data was collected from all four stacks over the testing period. The data was collected during the NO x Relative Variability Index testing project. 

# Executive Summary Table Stack A Stack B Stack C Stack D Combined Data collection period 3/12-14/08 3/12-14/08 3/20-22/08 3/12-14/08 3/17-22/08 3/17-22/08 3/17-20/08 3/17-22/08 Average S02 Emission Rate, 8.9 7.0 5.3 4.6 25.7 lb/hr Fired Pellet Production Rate, LTPH 235.9 (testing period average) Emission Factor, S02 lb/LT Fired Pellet 0.113 (testing period average)

23 69C06003 - I

# Introduction

Barr Engineering conducted sulfur dioxide (SOz) emissions engineering testing at ArcelorMittal Minorca Mine, Inc. (ArcelorMittal) located in Virginia, Minnesota. The test was performed to evaluate the SOz emissions as it relates to the normal operation of taconite production. The test simultaneously measured the emissions from the three of the four indurating furnace waste gas stacks during the NO x 

# relative variability index testing. A test plan was created but not submitted to the Minnesota Pollution Control Agency (MPCA). A copy of the internal use test plan is provided in Appendix G. Pete Rossmiller and Aaron Aamold of Barr Engineering performed the SOz testing. Jaime Baggenstoss and Jon Maki of ArcelorMittal coordinated the test team and facility operations. A list of project participants is provided in Appendix H. During the test, the indurating furnace was operated under normal operating conditions. The process operating data is provided in Appendix F.

2369C06003-1 

# 2 

# Introduction

Barr Engineering conducted sulfur dioxide (S02) emissions engineering testing at ArcelorMittal Minorca Mine, Inc. (ArcelorMittal) located in Virginia, Minnesota. The test was performed to evaluate the S02 emissions as it relates to the normal operation of taconite production. The test simultaneously measured the emissions from the three of the four indurating furnace waste gas stacks during the NO x 

# relative variability index testing. A test plan was created but not submitted to the Minnesota Pollution Control Agency (MPCA). A copy of the internal use test plan is provided in Appendix G. Pete Rossmiller and Aaron Aamold of Barr Engineering performed the SOz testing. Jaime Baggenstoss and Jon Maki of ArcelorMittal coordinated the test team and facility operations. A list of project participants is provided in Appendix H. During the test, the indurating furnace was operated under normal operating conditions. The process operating data is provided in Appendix F.

2369C06003-J 

# 2

# Results Testing of ArcelorMittal's pellet indurating furnace waste gas stacks began on March 11, 2008 and continued until March 22, 2008. There were several significant interruptions of data collection due to a plant breakdown and testing equipment failures. An interruption occurred with a plant shutdown on March 14 at 6:30 p.m. and continued until the plant was restarted and the furnace process stabilized on March 17 at 5:00 p.m. The primary problems with the test equipment were with the airflow measuring equipment. Several times moisture migrated into the pitot lines and froze giving false readings. Affected data was flagged when the problem appeared until the problem was corrected. S02 testing continued with the NO x RVI tests. Periods of process shutdown and invalidated hours due to instrument failure are identified in the dataset. The S02 analyzer located on Stack C (SVO16) failed to continuously output the correct signal to the data logger. Data was not collected on stack C until March 20 at 1:00 p.m. when stack B S02 analyzer was moved to Stack C. Data interpolation was performed to estimate the S02 concentration of Stack C from March 11 through March 20 and from March 20 to March 22 on Stack B. A discussion of the procedure used to estimate the concentrations is provided in Appendix A. Interpolated concentration data was used to generate Ib/hr emission using measured airflow from that stack. Forty-five minutes of acceptable data in an hour was used to represent one hour of valid data as would be allowed by a CEMS system. This allowed normal daily analyzer drift checks to be performed without omission of data as long as the procedure could be completed in fifteen minutes. Similarly, when sample gas filters required changing, the procedure was normally completed in less than fifteen minutes. These events are identified in the data spreadsheet. The data collection system used during the test experienced an occasional fault. As a result, the system recorded a significantly lower value for each parameter during a ten second averaging period. This error occurred nine times during the testing. In cases where it was obviously a data collection error, the fifteen-minute average was calculated using fourteen minutes of unaffected data. The result has a minimal effect on the data as only one minute out of sixty minutes during that hour was excluded. This exclusion is much less than the fifteen minute exclusion described above.

2369C06003-1 

# 3 

# Results Testing of ArcelorMittal's pellet indurating furnace waste gas stacks began on March 11, 2008 and continued until March 22, 2008. There were several significant interruptions of data collection due to a plant breakdown and testing equipment failures. An interruption occurred with a plant shutdown on March 14 at 6:30 p.m. and continued until the plant was restarted and the furnace process stabilized on March 17 at 5 :00 p.m. The primary problems with the test equipment were with the airflow measuring equipment. Several times moisture migrated into the pitot lines and froze giving false readings. Affected data was flagged when the problem appeared until the problem was corrected. S02 testing continued with the NO x RVI tests. Periods of process shutdown and invalidated hours due to instrument failure are identified in the dataset. The S02 analyzer located on Stack C (SVO 16) failed to continuously output the correct signal to the data logger. Data was not collected on stack C until March 20 at 1:00 p.m. when stack B S02 analyzer was moved to Stack C. Data interpolation was performed to estimate the S02 concentration of Stack C from March 11 through March 20 and from March 20 to March 22 on Stack B. A discussion of the procedure used to estimate the concentrations is provided in Appendix A. Interpolated concentration data was used to generate lb/hr emission using measured airflow from that stack. Forty-five minutes of acceptable data in an hour was used to represent one hour of valid data as would be allowed by a CEMS system. This allowed normal daily analyzer drift checks to be performed without omission of data as long as the procedure could be completed in fifteen minutes. Similarly, when sample gas filters required changing, the procedure was normally completed in less than fifteen minutes. These events are identified in the data spreadsheet. The data collection system used during the test experienced an occasional fault. As a result, the system recorded a significantly lower value for each parameter during a ten second averaging period. This error occurred nine times during the testing. In cases where it was obviously a data collection error, the fifteen-minute average was calculated using fourteen minutes of unaffected data. The result has a minimal effect on the data as only one minute out of sixty minutes during that hour was excluded. This exclusion is much less than the fifteen minute exclusion described above.

2369C06003-J 

# 3

# A copy of the data file "S02 Test data 3-11 through 3-22-08 Values.xls" is provided on a CD with this report. This dataset contains all of the test data and emission rate calculations. The one-hour data provided is calculated using fifteen-minute averages. Hard copies of the data were not printed due to the large volume of data. A summary of instrument output and resulting calculated emission rate are provided in Appendix C The variability index was not calculated since at no time was 

# S02 concentration data collected from all four stacks.

2369C06003-1 

# 4 A copy of the data file "S02 Test data 3-11 through 3-22-08 Values.xls" is provided on a CD with this report. This dataset contains all of the test data and emission rate calculations. The one-hour data provided is calculated using fifteen-minute averages. Hard copies of the data were not printed due to the large volume of data. A summary of instrument output and resulting calculated emission rate are provided in Appendix C The variability index was not calculated since at no time was 

# S02 concentration data collected from all four stacks.

2369C06003-J 

# 4

# Process description
ArcelorMittal mines taconite ore (magnetite) and produces iron pellets that are shipped to the company's blast furnaces in Indiana. The emission sources tested capture the waste gases from the pellet indurating process. Concentrate slurry flows to the thickener after which limestone is added for compression strength. The moisture of the concentrate is reduced by disk filters and then mixed with bentonite and conveyed to balling disks. Green balls produced on the balling disks are discharged to a roll screen to control the pellet size. The green balls are transferred to an oscillating conveyor and then to a roll conveyor for additional removal of less than Y4 inch material. The green balls are distributed evenly across the pallet cars, prior to entry into the pellet furnace. The pallet cars have a layer of fired pellets, called the hearth layer, on the bottom and sides of the car. The hearth layer allows for even airflow through the pellet bed and acts as a buffer between the pallet car and the heat generated through the exothermic conversion of magnetite to hematite. There is one natural gas fired furnace at ArcelorMittal's taconite plant. The straight grate furnace has several distinct zones. The first two stages are updraft and downdraft drying zones. The next zones are the preheat zone and firing zone. The temperature increases as the pellets pass through each zone reaching a peak in the firing zone. The pellets enter the after-firing zone, where the conversion of magnetite to hematite is completed. The last two zones are cooling zones that allow the pellets to be discharged at a temperature of around 120 degrees Fahrenheit. Heated air discharged from the two cooling zones is recirculated to the first zones of the furnace for drying and preheating the green balls. Off-gases from the furnaces are vented primarily through two ducts, the hood exhaust that handles the drying and recirculated cooling gases, and the windbox exhaust handles the preheat, firing, and after-firing gases. The windbox exhaust flows through a multiclone, which protects a downstream fan, and then is combined with the hood exhaust stream into a common header. The exhaust gases are subsequently divided into four streams which lead to four venturi rod scrubbers and exhaust from individual stacks.

2369C06003-1 

# 5 

# Process description
ArcelorMittal mines taconite ore (magnetite) and produces iron pellets that are shipped to the company's blast furnaces in Indiana. The emission sources tested capture the waste gases from the pellet indurating process. Concentrate slurry flows to the thickener after which limestone is added for compression strength. The moisture of the concentrate is reduced by disk filters and then mixed with bentonite and conveyed to balling disks. Green balls produced on the balling disks are discharged to a roll screen to control the pellet size. The green balls are transferred to an oscillating conveyor and then to a roll conveyor for additional removal of less than**~** 

# inch material. The green balls are distributed evenly across the pallet cars, prior to entry into the pellet furnace. The pallet cars have a layer of fired pellets, called the hearth layer, on the bottom and sides of the car. The hearth layer allows for even airflow through the pellet bed and acts as a buffer between the pallet car and the heat generated through the exothermic conversion of magnetite to hematite. There is one natural gas fired furnace at ArcelorMittal's taconite plant. The straight grate furnace has several distinct zones. The first two stages are updraft and downdraft drying zones. The next zones are the preheat zone and firing zone. The temperature increases as the pellets pass through each zone reaching a peak in the firing zone. The pellets enter the after-firing zone, where the conversion of magnetite to hematite is completed. The last two zones are cooling zones that allow the pellets to be discharged at a temperature of around 120 degrees Fahrenheit. Heated air discharged from the two cooling zones is recirculated to the first zones of the furnace for drying and preheating the green balls. Off-gases from the furnaces are vented primarily through two ducts, the hood exhaust that handles the drying and recirculated cooling gases, and the windbox exhaust handles the preheat, firing, and after-firing gases. The windbox exhaust flows through a multiclone, which protects a downstream fan, and then is combined with the hood exhaust stream into a common header. The exhaust gases are subsequently divided into four streams which lead to four venturi rod scrubbers and exhaust from individual stacks.

2369C06003-J 

# 5

# Stack testing procedures and methods
The testing was performed from ports meeting EPA Method 1 criteria. Test port location and full traverse drawings are provided in Figures 1 and 4. An initial airflow using an S-type pitot was performed using EPA Method 2 criteria at each stack. An S-type pitot tube was fixed at the point in the stack most representative of the average differential pressure. A calibrated Dwyer Magnesense gauge was used to read the differential pressure at this point. Calibrated type "K" thermocouples were positioned in the stack to measure stack temperature. Calculations of volumetric airflow were made with fifteen-minute average data values for velocity pressure, temperature, barometric pressure, oxygen and carbon dioxide. Stack gas moisture was measured using an approximation method (wet bulb-dry bulb technique) from EPA Method 4. Several daily readings indicated that wet bulb temperatures were consistently one degree Fahrenheit less than dry bulb temperatures; therefore all subsequent moistures were calculated assuming a wet bulb one degree less than the measured dry bulb value. A single continuous static pressure sensor was placed in Stack A but malfunctioned. When the error was discovered static pressures were read at each stack on March 19 and those values were used for their respective stack airflow calculations for the entire test. This has little impact on the overall results since the static pressure does not affect the airflow significantly and changes to static should remain relative to one another. The oxygen and carbon dioxide concentrations of the stack gas were measured at one stack continuously during the testing, with daily measurements made at the other three stacks. The 

# 02/C02 analyzer was calibrated per EPA Method 3A and was fed a split gas stream off the NO x system. The oxygen and carbon dioxide concentrations used for calculation of gas stream molecular weights for the three stacks which had only spot checks were performed using the previous data set average until another reading was taken. Sulfur dioxide concentrations were determined using a modified EPA Method 6C. Protocol 1 gas standards were used for daily instrument calibration, system bias checks. Analyzers were calibrated at the beginning of the project and after the plant shutdown. No intermediate instrument calibration adjustments were performed. The upper span gas used to determine maximum drift and system bias was 18.4 ppm S02. A single system bias was performed at the beginning of the project for each analyzer system. Subsequent calibrations were performed at the analyzers to conserve time on the NO x data collection. No bias corrections were made to the S02 data.

2369C06003-1 

# 6 

# Stack testing procedures and methods
The testing was performed from ports meeting EPA Method 1 criteria. Test port location and full traverse drawings are provided in Figures I and 4. An initial airflow using an S-type pitot was performed using EPA Method 2 criteria at each stack. An S-type pitot tube was fixed at the point in the stack most representative of the average differential pressure. A calibrated Dwyer Magnesense gauge was used to read the differential pressure at this point. Calibrated type "K" thermocouples were positioned in the stack to measure stack temperature. Calculations of volumetric airflow were made with fifteen-minute average data values for velocity pressure, temperature, barometric pressure, oxygen and carbon dioxide. Stack gas moisture was measured using an approximation method (wet bulb-dry bulb technique) from EPA Method 4. Several daily readings indicated that wet bulb temperatures were consistently one degree Fahrenheit less than dry bulb temperatures; therefore all subsequent moistures were calculated assuming a wet bulb one degree less than the measured dry bulb value. A single continuous static pressure sensor was placed in Stack A but malfunctioned. When the error was discovered static pressures were read at each stack on March 19 and those values were used for their respective stack airflow calculations for the entire test. This has little impact on the overall results since the static pressure does not affect the airflow significantly and changes to static should remain relative to one another. The oxygen and carbon dioxide concentrations of the stack gas were measured at one stack continuously during the testing, with daily measurements made at the other three stacks. The 

# 02/C02 analyzer was calibrated per EPA Method 3A and was fed a split gas stream off the NO x system. The oxygen and carbon dioxide concentrations used for calculation of gas stream molecular weights for the three stacks which had only spot checks were performed using the previous data set average until another reading was taken. Sulfur dioxide concentrations were determined using a modified EPA Method 6C. Protocol I gas standards were used for daily instrument calibration, system bias checks. Analyzers were calibrated at the beginning of the project and after the plant shutdown. No intermediate instrument calibration adjustments were performed. The upper span gas used to determine maximum drift and system bias was 18.4 ppm S02. A single system bias was performed at the beginning of the project for each analyzer system. Subsequent calibrations were performed at the analyzers to conserve time on the NO x data collection. No bias corrections were made to the S02 data.

2369C06003-1 

# 6

# u. S. EPA test Methods 

# 1,2, 3A, 4 and 6C are found in 40 CFR Part 60, Appendix A. Analyzer calibration documentation is provided in Appendix B. Calibration documentation for the remaining instruments is provided in Appendix D. Copies of the gas certification analysis for S02, oxygen and carbon dioxide are provided in Appendix E. A Campbell Scientific CRI 000 with multiplex board data logger system was used to record the output signals from the differential pressure gauge (pitot), stack thermocouple, S02, oxygen, carbon dioxide concentrations and ambient temperature. The data logger was programmed to collect data every ten seconds and generate one-minute and fifteen-minute averages. Four fifteen-minute averages were averaged to make one-hour averages. Data was averaged into hourly values two ways. One approach was to maximize the number of valid one-hour data points within the data set, the other was to obtain on the hour averages to coincide with process data. Both versions are in the spreadsheet.

2369C06003-1 

# 7 

# U. S. EPA test Methods 

# 1,2, 3A, 4 and 6C are found in 40 CFR Part 60, Appendix A. Analyzer calibration documentation is provided in Appendix B. Calibration documentation for the remaining instruments is provided in Appendix D. Copies of the gas certification analysis for S02, oxygen and carbon dioxide are provided in Appendix E. A Campbell Scientific CRI 000 with multiplex board data logger system was used to record the output signals from the differential pressure gauge (pitot), stack thermocouple, S02, oxygen, carbon dioxide concentrations and ambient temperature. The data logger was programmed to collect data every ten seconds and generate one-minute and fifteen-minute averages. Four fifteen-minute averages were averaged to make one-hour averages. Data was averaged into hourly values two ways. One approach was to maximize the number of valid one-hour data points within the data set, the other was to obtain on the hour averages to coincide with process data. Both versions are in the spreadsheet.

2369C06003-J 

# 7

# Tables 

# Tables

# ArcelorMittal Mincora Mine Pellet Plant 

# TABLE 1 S02 Test Results Summary Barr Engineering Co December 5, 2008

Finished Total Emission Unit Pellets (P1) Emission Factor DatelTime Ib/hr 502 LTPH Ib/LT 3/12/080:00 27 228 0.120 3/12/08 1:00 27 223 0.120 3/12/082:00 33 218 0.153 3/12/083:00 27 220 0.121 3/12/084:00 20 231 0.087 3/12/085:00 24 228 0.106 3/12/086:00 25 225 0.109 3/12/087:00 31 218 0.143 3/12/088:00 33 3/12/08 9:00 26 3/12/0810:00 22 3/12/08 11:00 19 3/12/0812:00 18 3/12/0813:00 20 328 0.060 3/12/0814:00 19 346 0.054 3/12/08 15:00 18 225 0.079 3/12/08 16:00 14 364 0.038 3/12/0817:00 17 318 0.053 3/13/080:00 30 205 0.144 3/13/08 1:00 30 215 0.142 3/13/082:00 29 218 0.131 3/13/083:00 30 215 0.140 3/13/084:00 30 219 0.135 3/13/085:00 25 215 0.116 3/13/086:00 30 205 0.146 3/13/08 7:00 31 192 0.163 3/13/08 8:00 23 218 0.106 3/13/08 9:00 20 217 0.094 3/13/08 10:00 20 213 0.095 3/13/08 11:00 19 216 0.088 3/13/0812:00 21 223 0.096 3/13/08 13:00 16 234 0.070 3/13/0814:00 19 225 0.084 3/13/0815:00 17 226 0.073 3/13/0816:00 15 229 0.063 3/13/0817:00 18 231 0.077 3/13/08 18:00 18 233 0.078 3/13/08 19:00 18 229 0.077 3/13/08 20:00 21 231 0.090 3/13/0821:00 22 222 0.100 3/13/0822:00 17 239 0.073 3/13/08 23:00 26 224 0.118 3/14/080:00 27 227 0.119 3/14/08 1:00 26 229 0.113 3/14/082:00 19 232 0.083 3/14/083:00 22 231 0.097 3/14/084:00 26 230 0.112 ArcelorMittal Mincora Mine Pellet Plant

DatelTime 3/12/080:00 3/12/08 1:00 3/12/082:00 3/12/083:00 3/12/084:00 3/12/085:00 3/12/086:00 3/12/087:00 3/12/088:00 3/12/08 9:00 3/12/0810:00 3/12/08 11 :00 3/12/0812:00 3/12/0813:00 3/12/0814:00 3/12/08 15:00 3/12/08 16:00 3/12/0817:00 3/13/080:00 3/13/08 1:00 3/13/082:00 3/13/083:00 3/13/084:00 3/13/085:00 3/13/086:00 3/13/08 7:00 3/13/08 8:00 3/13/08 9:00 3/13/08 10:00 3/13/08 11 :00 3/13/0812:00 3/13/08 13:00 3/13/0814:00 3/13/0815:00 3/13/0816:00 3/13/0817:00 3/13/08 18:00 3/13/08 19:00 3/13/08 20:00 3/13/0821:00 3/13/0822:00 3/13/08 23:00 3/14/080:00 3/14/08 1:00 3/14/082:00 3/14/083:00 3/14/084:00 

# TABLE 1 S02 Test Results Summary Finished Total Emission Unit Pellets (P1) Ib/hr 502 LTPH 27 228 27 223 33 218 27 220 20 231 24 228 25 225 31 218 33 26 22 19 18 20 328 19 346 18 225 14 364 17 318 30 205 30 215 29 218 30 215 30 219 25 215 30 205 31 192 23 218 20 217 20 213 19 216 21 223 16 234 19 225 17 226 15 229 18 231 18 233 18 229 21 231 22 222 17 239 26 224 27 227 26 229 19 232 22 231 26 230 Emission Factor Ib/LT 0.120 0.120 0.153 0.121 0.087 0.106 0.109 0.143

0.060 0.054 0.079 0.038 0.053 0.144 0.142 0.131 0.140 0.135 0.116 0.146 0.163 0.106 0.094 0.095 0.088 0.096 0.070 0.084 0.073 0.063 0.077 0.078 0.077 0.090 0.100 0.073 0.118 0.119 0.113 0.083 0.097 0.112 Barr Engineering Co December 5, 2008

# ArcelorMittal Mincora Mine Pellet Plant 

# TABLE 1 S02 Test Results Summary Barr Engineering Co December 5, 2008

Finished Total Emission Unit Pellets (P1) Emission Factor 

# DatelTime Ib/hr 502 LTPH Ib/LT 

# 3/14/08 5:00 27 224 0.121 3/14/086:00 28 228 0.122 3/14/087:00 33 222 0.151 3/14/088:00 29 222 0.132 3/14/08 9:00 30 219 0.137 3/14/0810:00 31 219 0.143 3/14/08 11:00 32 201 0.158 3/14/0818:00 30 217 0.139 3/14/0819:00 28 217 0.131 3/14/08 20:00 27 223 0.121 3/17/0815:00 23 3/17/0816:00 21 3/17/0817:00 17 3/17/0818:00 21 3/17/0819:00 21 3/17/0820:00 24 3/18/08 11:00 31 232 0.132 3/18/0812:00 29 299 0.098 3/18/08 13:00 28 222 0.128 3/18/0814:00 31 225 0.135 3/18/08 15:00 30 224 0.134 3/18/0816:00 32 225 0.142 3/18/0817:00 34 221 0.152 3/18/08 18:00 38 215 0.179 3/18/08 19:00 41 197 0.206 3/18/08 20:00 41 200 0.204 3/18/0821:00 39 199 0.198 3/18/08 22:00 30 204 0.145 3/18/08 23:00 24 218 0.109 3/19/080:00 24 282 0.084 3/19/08 1:00 17 307 0.055 3/19/08 2:00 13 270 0.048 3/19/08 3:00 11 240 0.047 3/19/08 4:00 12 227 0.052 3/19/08 5:00 10 223 0.046 3/19/086:00 11 224 0.051 3/19/08 7:00 11 229 0.050 3/19/08 8:00 22 231 0.096 3/19/089:00 23 305 0.074 3/19/08 10:00 21 230 0.089 3/19/08 11:00 25 234 0.107 3/19/0812:00 23 327 0.069 3/19/08 13:00 23 243 0.095 3/19/0814:00 25 227 0.112 3/19/08 15:00 27 233 0.114 3/19/08 16:00 24 230 0.106 3/19/0817:00 26 320 0.081 ArcelorMitlal Mincora Mine Pellet Plant

DatelTime 

# 3114/08 5:00 3/14/086:00 3/14/087:00 3/14/088:00 3/14/08 9:00 3/14/0810:00 3/14/08 11 :00 

# 3/14/0818:00 3/14/0819:00 3/14/08 20:00 3/17/0815:00 3/17/0816:00 3/17/0817:00 3/17/0818:00 3/17/0819:00 3/17/0820:00 3/18/08 11 :00 

# 3/18/0812:00 3/18/08 13:00 3/18/0814:00 3/18/08 15:00 3/18/0816:00 3/18/0817:00 3/18/08 18:00 3/18/08 19:00 3/18/08 20:00 3/18/0821:00 3/18/08 22:00 3/18/08 23:00 3/19/080:00 3/19/08 1 :00 

# 3/19/08 2:00 3/19/08 3:00 3/19/08 4:00 3/19/08 5:00 3/19/086:00 3/19/08 7:00 3/19/08 8:00 3/19/089:00 3/19/08 10:00 

# 3/19/08 11 :00 

# 3/19/0812:00 3/19/08 13:00 3/19/0814:00 3/19/08 15:00 3/19/08 16:00 3/19/0817:00 

# TABLE 1 S02 Test Results Summary Finished Total Emission Unit Pellets (P1) Ib/hr 502 LTPH 27 224 28 228 33 222 29 222 30 219 31 219 32 201 30 217 28 217 27 223 23 21 17 21 21 24 31 232 29 299 28 222 31 225 30 224 32 225 34 221 38 215 41 197 41 200 39 199 30 204 24 218 24 282 17 307 13 270 11 240 12 227 10 223 11 224 11 229 22 231 23 305 21 230 25 234 23 327 23 243 25 227 27 233 24 230 26 320 

# Emission Factor Ib/LT 0.121 0.122 0.151 0.132 0.137 0.143 0.158 0.139 0.131 0.121

0.132 0.098 0.128 0.135 0.134 0.142 0.152 0.179 0.206 0.204 0.198 0.145 0.109 0.084 0.055 0.048 0.047 0.052 0.046 0.051 0.050 0.096 0.074 0.089 0.107 0.069 0.095 0.112 0.114 0.106 0.081 Barr Engineering Co December 5, 2008

# ArcelorMittal Mincora Mine Pellet Plant 

# TABLE 1 S02 Test Results Summary Barr Engineering Co December 5, 2008

Finished Total Emission Unit Pellets (P1) Emission Factor Daterrime Ib/hr 502 LTPH Ib/LT 3/19/08 18:00 25 234 0.108 3/19/08 19:00 31 252 0.122 3/19/08 20:00 31 286 0.108 3/19/0821:00 29 224 0.128 3/19/08 22:00 25 216 0.115 3/19/08 23:00 24 221 0.109 3/20/08 0:00 23 279 0.082 3/20/08 1:00 21 294 0.072 3/20/08 2:00 20 255 0.078 3/20/08 3:00 18 318 0.055 3/20/08 4:00 22 294 0.075 3/20/08 5:00 30 265 0.113 3/20/08 6:00 29 252 0.115 3/20/08 7:00 25 235 0.107 3/20/08 8:00 27 231 0.115 3/20/08 9:00 31 225 0.139 3/20/0810:00 34 222 0.153 3/20/08 11:00 32 227 0.142 3/20/08 12:00 40 222 0.182 3/20/08 13:00 43 235 0.185 3/20/0814:00 39 287 0.136 3/20/08 15:00 39 230 0.171 3/20/0816:00 42 236 0.178 3/20/0817:00 40 225 0.177 3/20/08 18:00 31 213 0.145 3/20/08 19:00 32 209 0.155 3/20/08 20:00 28 211 0.134 3/20/08 21:00 30 220 0.136 3/20/08 22:00 34 209 0.160 3/20/08 23:00 29 218 0.131 3/21/080:00 21 228 0.094 3/21/081:00 26 219 0.117 3/21/082:00 29 220 0.130 3/21/083:00 27 232 0.118 3/21/084:00 29 275 0.105 3/21/085:00 24 235 0.104 3/21/086:00 33 219 0.150 3/21/087:00 29 217 0.135 3/21/08 8:00 26 222 0.117 3/21/089:00 30 226 0.132 3/21/0810:00 22 224 0.100 3/21/08 11:00 19 233 0.082 3/21/0812:00 21 235 0.089 3/21/0813:00 19 225 0.086 . 3/21/08 14:00 23 229 0.100

3/21/0815:00 21 234 0.090 3/21/0816:00 22 238 0.091 ArcelorMittal Mincora Mine Pellet Plant

Daterrime 3/19/08 18:00 3/19/08 19:00 3/19/08 20:00 3/19/0821:00 3/19/08 22:00 3/19/08 23:00 3/20/08 0:00 3/20/08 1:00 3/20/08 2:00 3/20/08 3:00 3/20/08 4:00 3/20/08 5:00 3/20/08 6:00 3/20/08 7:00 3/20/08 8:00 3/20/08 9:00 3/20/0810:00 3/20/08 11 :00 3/20/08 12:00 3/20/08 13:00 3/20/0814:00 3/20/08 15:00 3/20/0816:00 3/20/0817:00 3/20/08 18:00 3/20/08 19:00 3/20/08 20:00 3/20/08 21 :00 3/20/08 22:00 3/20/08 23:00 3/21/080:00 3/21/081:00 3/21/082:00 3/21/083:00 3/21/084:00 3/21/085:00 3/21/086:00 3/21/087:00 3/21/08 8:00 3/21/089:00 3/21/0810:00 3/21/08 11 :00 3/21/0812:00 3/21/0813:00

. 3/21/08 14:00

3/21/0815:00 3/21/0816:00 

# TABLE 1 S02 Test Results Summary Finished Total Emission Unit Pellets (P1) Ib/hr 502 LTPH 25 234 31 252 31 286 29 224 25 216 24 221 23 279 21 294 20 255 18 318 22 294 30 265 29 252 25 235 27 231 31 225 34 222 32 227 40 222 43 235 39 287 39 230 42 236 40 225 31 213 32 209 28 211 30 220 34 209 29 218 21 228 26 219 29 220 27 232 29 275 24 235 33 219 29 217 26 222 30 226 22 224 19 233 21 235 19 225 23 229 21 234 22 238 Emission Factor Ib/LT 0.108 0.122 0.108 0.128 0.115 0.109 0.082 0.072 0.078 0.055 0.075 0.113 0.115 0.107 0.115 0.139 0.153 0.142 0.182 0.185 0.136 0.171 0.178 0.177 0.145 0.155 0.134 0.136 0.160 0.131 0.094 0.117 0.130 0.118 0.105 0.104 0.150 0.135 0.117 0.132 0.100 0.082 0.089 0.086 0.100 0.090 0.091 Barr Engineering Co December 5, 2008

# ArcelorMittal Mincora Mine Pellet Plant 

# TABLE 1 S02 Test Results Summary Barr Engineering Co December 5,2008

Finished Total Emission Unit Pellets (P1) Emission Factor DatelTime Ib/hr 502 LTPH Ib/LT 

# 3/21/0817:00 18 281 0.065 

# 3/21/0818:00 21 227 0.094 

# 3/21/0819:00 27 308 0.087 

# 3/21/0820:00 27 278 0.098 

# 3/21/0821 :00 32 240 0.134 

# 3/21/0822:00 30 222 0.133 

# 3/21/0823:00 29 229 0.126 

# 3/22/08 0:00 26 226 0.116 

# 3/22/08 1:00 29 229 0.128 

# 3/22/08 2:00 29 223 0.132 

# 3/22/08 3:00 31 217 0.143 

# 3/22/08 4:00 23 234 0.099 

# 3/22/08 5:00 24 228 0.103 

# 3/22/08 6:00 24 228 0.107 

# 3/22/08 7:00 26 233 0.113 

# 3/22/08 8:00 30 219 0.139

Average 25.7 235.9 0.113 

# ArcelorMittal Mincora Mine Pellet Plant

DatelTime 3/21/0817:00 3/21/0818:00 3/21/0819:00 3/21/0820:00 3/21/0821 :00 3/21/0822:00 3/21/0823:00 3/22/08 0:00 3/22/08 1:00 3/22/08 2:00 3/22/08 3:00 3/22/08 4:00 3/22/08 5:00 3/22/08 6:00 3/22/08 7:00 3/22/08 8:00

Average 

# TABLE 1 S02 Test Results Summary Finished Total Emission Unit Pellets (P1) Ib/hr 502 LTPH 

# 18 281 21 227 27 308 27 278 32 240 30 222 29 229 26 226 29 229 29 223 31 217 23 234 24 228 24 228 26 233 30 219 25.7 235.9 Emission Factor Ib/LT 

# 0.065 0.094 0.087 0.098 0.134 0.133 0.126 0.116 0.128 0.132 0.143 0.099 0.103 0.107 0.113 0.139 0.113 Barr Engineering Co December 5,2008

# Figures Figures

# 101.75"

2 TEST PORTS @ 

# 90' 

# -t ....,30' 

# o 

# _!

r TESTING PLATFORM ELEVATION

FROM SCRUBBER

NOT TO SCALE 

# TEST PORT LOCATIONS ARCELORMITIAL MINORCA MINE, INC. VIRGINIA, MINNESOTA PELLET INDURATING FURNACE (SV014,015), (EU026) FIGURE 1 NOT TO SCALE 2 TEST PORTS @ 

# 90' 101.75" 

# -t ,-..,30' 

# 0- 

# 1
TESTING PLATFORM ELEVATION 

# l'

TEST PORT LOCATIONS ARCELORMITIAL MINORCA MINE, INC. VIRGINIA, MINNESOTA FROM SCRUBBER



# PELLET INDURATING FURNACE (SV014,015), (EU026) FIGURE 1

# •
•

• • 

# • •



# •

•
• • • 

# •

NO. OF TEST PORTS PORT LENGTH PORT DIAMETER NO. OF TRAVERSE POINTS DUCT DIAMETER 

# 2 6.0" 4.0"

12 101.75" POINT INSERTION DEPTH IN " 1 4.43 2 14.90 3 30.11 4 71.64 5 86.85 6 97.32



# TRAVERSE POINT LOCATIONS ARCELORMITIAL MINORCA MINE, INC. VIRGINIA, MINNESOTA PELLET INDURATING FURNACE (SV014,015), (EU026) NOT TO SCALE 

# FIGURE 2 

# • • •

• • 

# • • •



# • • •

POINT NO. OF TEST PORTS 2 1 PORT LENGTH 6.0" 2 PORT DIAMETER 4.0" 3 NO. OF TRAVERSE POINTS 12 DUCT DIAMETER 101.75" 4 5 6



# TRAVERSE POINT LOCATIONS ARCELORMITIAL MINORCA MINE, INC. VIRGINIA, MINNESOTA 

# •

INSERTION DEPTH IN " 4.43 14.90 30.11 71.64 86.85 97.32



# PELLET INDURATING FURNACE (SV014,015), (EU026) NOT TO SCALE 

# FIGURE 2

# 105.0"

2 TEST PORTS @ 

# 90' 

# -t ""30' 

# o

# -~ TESTING PLATFORM ELEVATION

FROM SCRUBBER



# TEST PORT LOCATIONS ARCELORMITIAL MINORCA MINE, INC. VIRGINIA, MINNESOTA PELLET INDURATING FURNACE (SV016,017), (EU026) NOT TO SCALE 

# FIGURE 3 NOT TO SCALE 2 TEST PORTS @ 

# 90' 105.0"

# -t rv30' 

# o

# -~ TESTING PLATFORM ELEVATION



# TEST PORT LOCATIONS ARCELORMITIAL MINORCA MINE, INC. VIRGINIA, MINNESOTA FROM SCRUBBER



# PELLET INDURATING FURNACE (SV016,017), (EU026) FIGURE 3

# •


# •

• 

# • • 

# •

•

•
• 

# • • •

NO. OF TEST PORTS PORT LENGTH PORT DIAMETER NO. OF TRAVERSE POINTS DUCT DIAMETER 

# 2 6.0" 4.0"

12 105.0" POINT INSERTION DEPTH IN " 

# 1 4.57 2 15.38 3 31.07 4 73.93 5 89.62 6 100.43



# TRAVERSE POINT LOCATIONS ARCELORMITIAL MINORCA MINE, INC. VIRGINIA, MINNESOTA PELLET INDURATING FURNACE (SV016,017), (EU026) NOT TO SCALE 

# FIGURE 4 

# • 

# •

NO. OF TEST PORTS PORT LENGTH PORT DIAMETER NO. OF TRAVERSE POINTS DUCT DIAMETER 

# •

2 6.0" 4.0"

12 105.0" 

# • 

# • •

• •

• • •

POINT 

# 1 2 3 4 5 6



# TRAVERSE POINT LOCATIONS ARCELORMITIAL MINORCA MINE, INC. VIRGINIA, MINNESOTA 

# •

INSERTION DEPTH IN " 

# 4.57 15.38 31.07 73.93 89.62 100.43



# PELLET INDURATING FURNACE (SV016,017), (EU026) NOT TO SCALE 

# FIGURE 4

# Appendices Appendices

# Appendix A Report Calculations and Nomenclature 

# Appendix A Report Calculations and Nomenclature

# Arcelor Mittal Pellet Plant Virginia, MN 

# Example Calculation Results of S02 Volumetric Airflow Rate Determination Data From 12/8/2008 midnight-Row 112 OnNox spreadsheet 

# Barr Engineering Co. May 16, 2008

Data Entry Symbol Units Stack A Stack B Stack C Stack D ITest Date 

# - - 3/12/2008 3/12/2008 3/12/2008 3/12/2008 Pitot Tube Coefficient Cp 

# - 0.84 0.84 0.84 0.84 Number of Sample Ports 

# - 

# - 1 1 1 1 Number of Traverse Points 

# - 

# - Single Avg. Single Avg. Single Avg. Single Avg. Duct Dimensions (diameter for circular duct) D inches 101.75 101.75 105 105 Barometric Pressure Pbar in. Hg 28.09 28.09 28.09 28.09

- 

# Stack Static Pressure from Static Pressure Sensor Pg in. H2O -0.80 -0.65 -0.60 -0.75 Average Stack Temperature, dry bulb Tsf degrees F 114 112 119 125 Averagge Stack Temperature, wet bulb Tswf degrees F 113 111 118 124 Average Delta P from Diffemtal Pressure Sensor boP in H2O 0.986 0.773 0.780 0.980

---- 

# Average Square Root of Velocity Head (boP)AO.5 

# - 0.993 0.879 0.883 0.990 

# _. Orsat Results, Dry Basis (Method 3A) Carbon dioxide %0 2 

# %v/v 1.3 1.5 2.0 2.4 Oxygen %C0 2 

# %v/v 19.3 18.6 18.4 18.1 Carbon Monoxide + Nitrogen - %v/v 79.4 79.9 79.6 79.5 Calculated Data Symbol Units Run A Run B Run C Run D Duct Area A 

# = (D/24)A2 x PI (Circular Duct) A sq 

# ft 56.47 56.47 60.13 60.13 A 

# = (L x W)/144 (Rectangular Duct) Stack Pressure Ps in Hg 28.03 28.04 28.05 28.03 Ps 

# = Pbar + Pg/13.6 ---'- 

# Average Moisture Content of Stack Gas MC % Vol 10.075 9.335 11.415 13.741 see below Molecular Weight of Stack Gas, dry Md Ibllbmol 28.98 28.98 29.06 29.11 Md 

# = (0.44 x (%C02))+(0.32 x (%02))+(0.28 x (%N2+%CO))**~--,._---** 

# Molecular Weight of Stack Gas, wet Ms Ibl!bmol 27.87 27.96 27.79 27.58**~s:==** 

# Md x (1-(MC/100))+18 x (MC/100) Average Stack Gas Velocity Vs ftlsec 61.13 53.91 54.65 61.85 Vs 

# = 85.49 x Cp x (boPjAO.5 x «(Ts+460)/Ps x Ms)A.5) Actual Volumetric Flowrate Qa acfm 207,100 182,600 197,200 223,200 Qa 

# = 60xVs xA

-- 

# Volumetric Flowrate at Standard Conditions Qs scfm 178,400 158,100 168,700 188,600 Qs 

# = Qa x (528/(Ts+460)) x (Ps/29.92) Dry Volumetric Flowrate at Standard Conditions Qd dscfm 160,439 143,329 149,401 162,711 Qd 

# = Qa x (1-(MC/100)) x (528/(Ts+460)) x (Ps/29.92) Moisture Calculation 1 00*«(0.1804*1 OA«7.5*«WB-32)/1.8))/(237.7+«WB-32)/1.8))))-(0.000367*Stack Pressure, in Hg*(DB-WB)*(1+«WB-32)/1571 ))))/Stack Pressure, in Hg) 

# Arcelor Mittal Pellet Plant Virginia, MN 

# Example Calculation Results of S02 Volumetric Airflow Rate Determination Data From 

# 12/8/2008 midnight-Row 112 On Nox spreadsheet Data Entry Symbol Units Stack A ITest Date 

# - - 3/12/2008 Pitot Tube Coefficient Cp 

# - 0.84 Number of Sample Ports 

# - 

# - 1 Number of Traverse Points 

# - 

# - Single Avg. Duct Dimensions (diameter for circular duct) D inches 101.75 Barometric Pressure Pbar in. Hg 28.09 Stack Static Pressure from Static Pressure Sensor Pg in. H2O -0.80 Average Stack Temperature, dry bulb Tsf degrees F 114 Averagge Stack Temperature, wet bulb Tswf degrees F 113 Average Delta P from Diffemtal Pressure Sensor boP in H2O 0.986 Average Square Root of Velocity Head (boP)AO.5 

# - 0.993 Orsat Results, Dry Basis (Method 3A) Carbon dioxide %0 2 

# %v/v 

# 1.3 Oxygen %C0 2 

# %v/v 

# 19.3 Carbon Monoxide + Nitrogen - %v/v 

# 79.4 Calculated Data Symbol Units Run A Duct Area A 

# = (D/24)A2 x PI (Circular Duct) A sq 

# ft 56.47 A 

# = (L x 

# W)/144 (Rectangular Duct) Stack Pressure Ps in Hg 28.03 Ps 

# = Pbar + 

# Pg/13.6 Average Moisture Content of Stack Gas MC % Vol 10.075 see below Molecular Weight of Stack Gas, dry Md Ibllbmol 28.98 Md 

# = (0.44 x (%C02))+(0.32 x (%02))+(0.28 x (%N2+%CO)) Molecular Weight of Stack Gas, wet Ms Ibl!bmol 27.87**~s** 

# = Md x 

# (1-(MC/100))+18 x 

# (MC/100) Average Stack Gas Velocity Vs ftlsec 61.13 Vs 

# = 85.49 x Cp x (boPjAO.5 x 

# (((Ts+460)/Ps x Ms)A.5) Actual Volumetric Flowrate Qa acfm 207,100 Qa 

# = 60xVs xA Volumetric Flowrate at Standard Conditions Qs scfm 178,400 Qs 

# = Qa x 

# (528/(Ts+460)) x 

# (Ps/29.92) Dry Volumetric Flowrate at Standard Conditions Qd dscfm 160,439 Qd 

# = Qa x 

# (1-(MC/100)) x 

# (528/(Ts+460)) x 

# (Ps/29.92) Moisture Calculation 

# Barr Engineering Co. May 16, 2008

Stack B Stack C Stack D 

# 3/12/2008 3/12/2008 3/12/2008

0.84 0.84 0.84

1 1 1 Single Avg. Single Avg. Single Avg.

101.75 105 105 28.09 28.09 28.09 -0.65 -0.60 -0.75 112 119 125 111 118 124 0.773 0.780 0.980

---- 

# 0.879 0.883 0.990

..



# 1.5 2.0 2.4 18.6 18.4 18.1 79.9 79.6 79.5 Run B Run C Run D 56.47 60.13 60.13 28.04 28.05 28.03

---- 

# 9.335 11.415 13.741 28.98 29.06 29.11

...

# _--- 27.96 27.79 27.58 53.91 54.65 61.85 182,600 197,200 223,200

.. 

# 158,100 168,700 188,600 143,329 149,401 162,711

100*(((0.1804*1 OA((7.5*((WB-32)/1.8))/(237.7+((WB-32)/1.8))))-(0.000367*Stack Pressure, in Hg*(DB-WB)*(1+((WB-32)/1571 ))))/Stack Pressure, in Hg)

# Calculation Equations - EPA Methods 3A, 6C
System bias adjustment on source concentration indicated by the analyzer. 

# C 

# =(C -C) CmA

ppm A 0 

# C C m - 0 

# where: is the adjusted source concentration, ppm(dry) is the average concentration indicated by the analyzer, ppm(dry) is the average of the initial and final system calibration responses of the zero gas, ppm is the average of the initial and final system calibration responses of the upscale gas, ppm is the certified concentration of the upscale calibration gas, ppm Convert source concentration into emission rate (Iblhr). 

# C _ 

# MWxCppm



# ( ...!!!LJ- 24.04 dscm


# E(/b/hr) 

# = (6.242 X 

# 10- 8 

# )x C( m g ) 

# X 

# 60 X 

# Qd dscm 

# where: 

# C(..!!!K-) dscm 

# MW



# 24.04 E(lblhr) 

# 6.242xlO· 8 

# Qd 

# 60 amount of compound, by weight(mg), per dry standard cubic meter of air is the molecular weight of the gaseous compound where MW = 

# is the molar volume of gas at 68 

# OF and 29.92 in Hg, L/g-mole emission rate of gaseous compound 

# in pounds per hour is the conversion factor from mg/rrr' to Ib/ft3 

# flow rate of 

# dry gas at standard conditions in cubic feet per minute, dscfrn is the conversion factor from minutes to hours

W:\Business Units\EM\Subunit Admin\Technical & 

# Support Services\AIR SAMPLING\Templates\Reports\Equations\analyzereq Compliance.doc 

# Calculation Equations

- EPA Methods 3A, 6C
System bias adjustment on source concentration indicated by the analyzer.

where: 

# C =(C -C) CiliA ppIII A 0 

# C C III - 

# 0


# is the adjusted source concentration, ppm(dry) is the average concentration indicated by the analyzer, ppm(dry) is the average of the initial and final system calibration responses ofthe zero gas, ppm is the average of the initial and final system calibration responses of the upscale gas, ppm is the certified concentration of the upscale calibration gas, ppm Convert source concentration into emission rate (lb/hr).

where: 

# C _ 

# MWXCPPIII 

# ( ..!!!LJ

- 24.04 dscm


# E(/b/h/") 

# = (6.242 X 

# 10- 8 

# )x C( mg ) 

# X 

# 60 X 

# Qd 

# dSCIII

# C(~) r.i'iCl1l 

# MW



# 24.04 E(lblhr) 

# 6.242xlO- 8 

# Qd 

# 60 amount of compound, by weight(mg), per dry standard cubic meter of air is the molecular weight of the gaseous compound where MW = 

# is the molar volume of gas at 68 

# OF and 29.92 in Hg, Llg-mole emission rate of gaseous compound 

# in pounds per hour is the conversion factor from mg/m3 to Ib/ft3 flow rate of 

# dry gas at standard conditions in cubic feet per minute, dscfrn is the conversion factor from minutes to hours

W:\Business Units\EM\Subunit Admin\Technical & 

# Support Services\AIR SAMPLING\Templates\Reports\Equations\analyzereq Compliance.doc

## ArcelorMittal Mincora Mine Pellet Plant Sulfur Dioxide Test Resutls Summary Furnace Line Waste Gas Stacks 8arr Engineering Co. December 5, 2008
Stack A Stack 8 Stack C Stack D Total Emission Unit Total Emission Unit Hourly Average Hourly Average Hourly Average Hourly Average 15 minute average On the hour Dateffime Iblhr S02 Iblhr S02 Iblhr S02 Iblhr S02 Iblhr S02 Iblhr S02 3/11/0823:45 25 3/12/08 0:00 27 27 3/12/080:15 23 3/12/08 0:30 9.03 6.91 ./.76 

## 3.84 24 3/12/08 0:45 31 3/12/08 1:DO 3D 27 3/12/081:15 33 3/12/08 1:30 11.46 8.88 6.01 

## 4.87 32 3/12/08 1:45 35 3/12/08 2:00 34 33 3/12/08 2:15 31 3/12/08 2:30 11.32 8.70 

## 6.33 5.38 28 3/12/08 2:45 25 3/12/08 3:DO 23 27 3/12/083:15 19 3/12/08 3:30 7.38 5.60**~,40** 

## 3.99 19 3/12/08 3:45 21 3/12/08 4:00 22 20 3/12/08 4:15 19 3/12/08 4:30 7.18 5.57**~.26** 

## 3.84 21 3/12/08 4:45 28 3/12/08 5:00 28 24 3/12/08 5:15 24 3/12/08 5:30 9.30 7.36 5.06 

## 4.13 23 3/12/08 5:45 25 3/12/08 6:00 27 25 3/12/086:15 31 3/12/08 6:30 10.22 8.21**5.~~** 

## 4.35 3D 3/12/08 6:45 31 3/12/087:00 33 31 3/12/087:15 35 3/12/08 7:30 11.98 9.63 6.52 

## 5.29 35 3/12/087:45 35 3/12/08 8:00 28 33 3/12/088:15 23 3/12/08 8:30 10.30 8.25 

## 5,41 4.24 26 3/12/08 8:45 29 3/12/08 9:00 27 26 3/12/08 9:15 26 3/12/08 9:30 10.07 7.74 5./0 

## 3.88 26 3/12/08 9:45 21 3/12/08 10:DO 17 22 3/12/08 10:15 17 3/12/08 10:30 5.84 4.79 

## 3.57 3.28 16 3/12/08 10:45 21 3/12/08 11:00 22 19 3/12/0811:15 18 3/12/08 11:30 6.69 5.26 

## 3.86 3.44 16 3/12/08 11:45 17 3/12/08 12:00 21 18 3/12/0812:15 20 3/12/08 12:30 6.19 5.03 

## 3.91 3.40 18 3/12/08 12:45 17 3/12/08 13:00 24 20 3/12/0813:15 20 3/12/08 13:30 6.54 4.65 

## 3.72 3.29 18 3/12/08 13:45 17 3/12/08 14:00 20 19 3/12/0814:15 21 3/12/08 14:30 7.49 5.20 

## 3.91 3.20 21 3/12/08 14:45 15 3/12/08 15:00 14 18 3/12/0815:15 14 3/12/08 15:30 5.23 3.92 2.87 

## 2.46 15 3/12/08 15:45 13 3/12/0816:00 13 14 3/12/08 16:15 14 3/12/08 16:30 4.71 3.93 

## 2.88 2.74 16 3/12/08 16:45 18 3/12/0817:00 20 17 3/12/0817:15 21 3/12/08 23:45 31 3/13/08 0:00 28 3D 3/13/08 0:15 33 3/13/08 0:30 11.52 9.01**~.83** 

## 5.17 3D 3/13/08 0:45 32 3/13/08 1:00 27 3D 3/13/081:15 27 3/13/08 1:30 10.59 7.68 6.07 

## 4.62 3D • Individual stack hourly data does not coincide with "on the hour" emission unit totals • hourly data in italics is generated using interpolated S02 concentration data ArcelorMittal Mincora Mine Pellet Plant

Dateffime 3/11/0823:45 3/12108 0:00 3/121080:15 3/12108 0:30 3/12108 0:45 3/12108 

## 1:00 3/121081:15 3/12108 

## 1 :30 3/12108 

## 1 :45 3/12108 2:00 3/12108 2:15 3/12108 2:30 3/12108 2:45 3/12108 3:00 3/121083:15 3/12108 3:30 3/12108 3:45 3/12108 4:00 3/12108 4:15 3/12108 4:30 3/12108 4:45 3/12108 5:00 3/12108 5:15 3/12108 5:30 3/12108 5:45 3/12108 6:00 3/121086:15 3/12108 6:30 3/12108 6:45 3/121087:00 3/121087:15 3/12108 7:30 3/121087:45 3/12108 8:00 3/121088:15 3/12108 8:30 3/12108 8:45 3/12108 9:00 3/12108 9:15 3/12108 9:30 3/12108 9:45 3/12108 

## 10:00 3/12108 

## 10:15 3/12108 

## 10:30 3/12108 

## 10:45 3/12108 

## 11 :00 3/1210811:15 3/12108 

## 11 :30 3/12108 

## 11 :45 3/12108 12:00 3/1210812:15 3/12108 12:30 3/12108 12:45 3/12108 13:00 3/1210813:15 3/12108 13:30 3/12108 13:45 3/12108 14:00 3/1210814:15 3/12108 14:30 3/12108 14:45 3/12108 15:00 3/1210815:15 3/12108 15:30 3/12108 15:45 3/1210816:00 3/12108 16:15 3/12108 16:30 3/12108 16:45 

## 3/1210817:00 3/1210817:15 3/12108 23:45 3/13/08 0:00 3/13/08 

## 0: 15 3/13/08 0:30 

## 3/13108 0:45 3113/08 

## 1 :00 31131081:15 3/13108 1 :30 Stack A Hourly Average

Iblhr S02

9.03

11.46

11.32

7.38

7.18

9.30

10.22

11.98

10.30

10.07

5.84

6.69

6.19

6.54

7.49

5.23

4.71

11.52

10.59 Sulfur Dioxide Test Resutls Summary Furnace Line Waste Gas Stacks Stack 8 Stack C Stack D Hourly Average Hourly Average Hourly Average

Iblhr S02 Iblhr S02 Iblhr S02

6.91 ./.76 

## 3.84

8.88 

## 6.01 4.87

8.70 

## 6.33 5.38

5.60**~AO** 

## 3.99

5.57**~.26** 

## 3.84

7.36 

## 5.06 4.13

8.21**5.~~** 

## 4.35

9.63 6.52 

## 5.29

8.25 

## 5AI 4.24

7.74 

## 5.10 3.88

4.79 

## 3.57 3.28

5.26 

## 3.86 3.44

5.03 

## 3.91 3.40

4.65 

## 3.72 3.29

5.20 

## 3.91 3.20

3.92 2.S7 

## 2.46

3.93 

## 2.88 2.74

9.01**~.83** 

## 5.17

7.68 6.07 

## 4.62

• Individual stack hourly data does not coincide with "on the hour" emission unit totals
• hourly data in italics is generated using interpolated S02 concentration data 8arr Engineering Co. December 5, 2008

Total Emission Unit Total Emission Unit 15 minute average On the hour Iblhr S02 Iblhr S02

25 27 27 23 24 31 30 27 33 32 35 34 33 31 28 25 23 27 19 19 21 22 20 19 21 28 28 24 24 23 25 27 25 31 30 31 33 31 35 35 35 28 33 23 26 29 27 26 26 26 21 17 22 17 16 21 22 19 18 16 17 21 18 20 18 17 24 20 20 18 17 20 19 21 21 15 14 18 14 15 13 13 14 14 16 18 20 17 21 31 28 3D 33 3D 32 27 30 27 3D

## ArcelorMitlal Mincora Mine Pellet Plant Sulfur Dioxide Test Resutis Summary Fumace Line Waste Gas Stacks Barr Engineering Co. December 5, 2008
Stack A Stack B Stack C Stack D Total Emission Unit Total Emission Unit Hourty Average Hourty Average Hourty Average Hourty Average 15 minute average On the hour Date/Time IblhrS02 Iblhr S02 IblhrS02 IblhrS02 Iblhr S02 Iblhr S02 3/13/08 1:45 30 3/13/08 2:00 28 29 3/13/082:15 28 3/13/08 2:30 10.52 7.50 6.41 4.60 30 3/13/08 2:45 30 3/13/08 3:00 31 30 3/13/083:15 31 3/13/08 3:30 11.75 8.60 4.46 5.76 30 3/13/08 3:45 31 3/13/08 4:00 26 30 3/13/084:15 24 3/13/08 4:30 10.57 7.46 4./9 4.40 25 3/13/08 4:45 26 3/13/08 5:00 26 25 3/13/085:15 27 3/13/08 5:30 10.07 7.45 4.95 3.95 28 3/13/08 5:45 32 3/13/08 6:00 33 30 3/13/086:15 34 3/13/08 6:30 11.04 9.08 5.36 7.13 32 3/13/08 6:45 30 3/13/087:00 30 31 3/13/087:15 28 3/13/08 7:30 9.72 7.68 6.26 4.37 24 3/13/087:45 20 3/13/08 8:00 20 23 3/13/088:15 19 3/13/08 8:30 7.60 5.86 

## 5.30 1.11 21 3/13/08 8:45 21 3/13/08 9:00 21 20 3113/089:15 22 3/13/08 9:30 9.49 6.84 

## 5.08 0.00 21 3/13/08 9:45 19 3/13/08 10:00 18 20 3/13/0810:15 19 3/13/08 10:30 8.91 6.40 3.53 0.00 19 3/13/08 10:45 21 3/13/08 11:00 17 19 3/13/0811:15 15 3/13/08 11:30 7.16 5.86 

## 3.70 0.00 25 3/13/08 11:45 24 3/13/08 12:00 22 21 3/13/0812:15 20 3/13/08 12:30 6.24 4.93 3.73 5.24 15 3/13/08 12:45 13 3/13/08 13:00 17 16 3/13/0813:15 21 3/13/08 13:30 5.02 4.08 .4.25 

## 4.39 20 3/13/08 13:45 16 3/13/08 14:00 19 19 3/13/0814:15 19 3/13/08 14:30 5.96 4.40 3.85 4.11 19 3/13/0814:45 14 3/13/08 15:00 14 17 3/13/0815:15 14 3/13/08 15:30 4.10 3.17 2.85 3.70 14 3/13/08 15:45 16 3/13/08 16:00 15 15 3/13/0816:15 16 3/13/08 16:30 5.31 3.97 2.83 3.64 16 3/13/08 16:45 20 3/13/0817:00 19 18 3/13/0817:15 19 3/13/0817:30 6.50 4.93 3.76 3.77 18 3/13/0817:45 18 3/13/0818:00 17 18 3/13/0818:15 18 3/13/08 18:30 5.64 4.89 

## 3.70 3.52 17 3/13/08 18:45 16 3/13/08 19:00 18 18 3/13/0819:15 20 3/13/08 19:30 5.94 5.05 3.66 3.63 17 3/13/08 19:45 21 3/13/08 20:00 25 21 3/13/0820:15 27 3/13/08 20:30 8.03 6.93 4.77 4.00 23 3/13/08 20:45 21 3/13/0821:00 18 22 3/13/0821:15 19 • Individual stack hourty data does not coincide with "on the hour" emission unit totals • hourty data in italics is generated using interpolated S02 concentration data 

## ArcelorMittal Mincora Mine Pellet Plant

Datemme 3/13/08 

## 1 :45 3/13/08 2:00 3/13/082:15 3/13/08 2:30 3/13/08 2:45 3/13/08 3:00 3/13/083:15 3/13/08 3:30 3/13/08 3:45 3/13/08 4:00 3/13/084:15 3/13/08 

## 4 :30 3/13/08 4:45 3/13/08 5:00 3/13/085:15 3/13/08 5:30 3/13/08 5:45 3/13/08 6:00 3/13/086:15 3/13/08 6:30 3/13/08 6:45 3/13/087:00 3/13/087:15 3/13/08 

## 7 :30 3/13/087:45 3/13/08 8:00 3/13/088:15 3/13/08 8:30 3/13/08 8:45 3/13/08 9:00 3113/089:15 3/13/08 9:30 3/13/08 9:45 3/13/08 

## 10:00 3/13/0810:15 3/13/08 

## 10:30 3/13/08 

## 10:45 3/13/08 

## 11 :00 3/13/0811:15 3/13/08 

## 11 :30 3/13/08 

## 11 :45 3/13/08 12:00 3/13/0812:15 3/13/08 12:30 3/13/08 12:45 3/13/08 13:00 3/13/0813:15 3/13/08 13:30 3/13/08 13:45 3/13/08 14:00 3/13/0814:15 3/13/08 14:30 3/13/0814:45 3/13/08 15:00 3/13/0815:15 3/13/08 15:30 3/13/08 15:45 3/13/08 16:00 3/13/0816:15 3/13/08 16:30 3/13/08 16:45 3/13/0817:00 3/13/0817:15 3/13/0817:30 3/13/0817:45 3/13/0818:00 3/13/0818:15 3/13/08 18:30 3/13/08 18:45 3/13/08 19:00 3/13/0819:15 3/13/08 19:30 3/13/08 19:45 3/13/08 20:00 3/13/0820:15 3/13/08 20:30 3/13/08 20:45 3/13/0821:00 3/13/0821:15 

## Stack A Hourty Average

IblhrS02

10.52

11.75

10.57

10.07

11.04

9.72

7.60

9.49

8.91

7.16

6.24

5.02

5.96

4.10

5.31

6.50

5.64

5.94

8.03 Sulfur Dioxide Test Resutls Summary Furnace Line Waste Gas Stacks Stack B Stack C Stack D Hourty Average Hourty Average Hourty Average

Iblhr S02 IblhrS02 IblhrS02

7.50 6AI 

## 4.60

8.60 

## 4.46 5.76

7.46 

## 4.19 4.40

7.45 

## 4.95 3.95

9.08 

## 5.36 7.13

7.68 

## 6.26 4.37

5.86 

## 5.30 1.11

6.84 

## 5.08 0.00

6.40 

## 3.53 0.00

5.86 

## 3.70 0.00

4.93 

## 3.73 5.24

4.08 ';,25 

## 4.39

4.40 

## 3.85 4.11

3.17 

## 2.85 3.70

3.97 

## 2.83 3.64

4.93 

## 3.76 3.77

4.89 

## 3.70 3.52

5.05 

## 3.66 3.63

6.93 4.il 

## 4.00

• Individual stack hourty data does not coincide with "on the hour" emission unit totals
• hourty data in italics is generated using interpolated S02 concentration data Barr Engineering Co. December 5, 2008

Total Emission Unit Total Emission Unit 15 minute average On the hour Iblhr S02 Iblhr S02

30 28 29 28 30 30 31 30 31 30 31 26 30 24 25 26 26 25 27 28 32 33 30 34 32 30 30 31 28 24 20 20 23 19 21 21 21 20 22 21 19 18 20 19 19 21 17 19 15 25 24 22 21 20 15 13 17 16 21 20 16 19 19 19 19 14 14 17 14 14 16 15 15 16 16 20 19 18 19 18 18 17 18 18 17 16 18 18 20 17 21 25 21 27 23 21 18 22 19

## ArcelorMittal Mincora Mine Pellet Plant Sulfur Dioxide Tesl Resulls Summary Furnace Line Wasle Gas Slacks 8arr Engineering Co. December 5, 2008
Stack A Slack 8 Slack C Stack D Total Emission Unit Total Emission Unit Hourly Average Hourly Average Houriy Average Houriy Average 15 minute average On the hour Date/Time Iblhr S02 Iblhr S02 IblhrS02 IblhrS02 Iblhr S02 Iblhr S02 3/13/08 21:30 6.22 5.29 3.94 

## 3.58 18 3/13/08 21:45 17 3/13/08 22:00 16 17 3/13/0822:15 20 3/13/08 22:30 6.59 5.76 4.12 

## 3.71 27 3/13/08 22:45 30 3/13/08 23:00 28 26 3/13/08 23:15 

## 25 3/13/08 23:30 

## 9.10 8.08 5. Ii 

## 4.23 24 3/13/08 23:45 

## 27 3/14/08 0:00 

## 34 27 3/14/08 0:15 

## 32 3/14/08 0:30 

## 10.16 9.43 5.89 

## 4,91 29 3/14/080:45 

## 23 3/14/08 

## 1:00 19 26 3/14/081:15 19 3/14/08 1:30 6.94 6,00 4.21 

## 3.67 22 3/14/08 1:45 21 3/14/082:00 16 19 3/14/08 2:15 20 3/14/08 2:30 6.43 5.28 4.02 

## 3.61 21 3/14/08 2:45 25 3/14/08 3:00 24 22 3/14/083:15 

## 25 3/14/08 3:30 

## 8.43 7.25 4.9i 

## 4.22 25 3/14/08 3:45 26 3/14/084:00 

## 26 26 3/14/084:15 29 3/14/084:30 

## 9.02 7.93 5.27 

## 4.40 26 3/14/084:45 28 3/14/08 5:00 25 27 3/14/08 5:15 25 3/14/08 5:30 8.92 8.11 

## 5.22 4.40 28 3/14/08 5:45 

## 29 3/14/08 6:00 

## 30 28 3/14/086:15 

## 32 3/14/08 6:30 

## 10.14 9.29 6.20 

## 5.41 

# 34 3/14/086:45 

## 36 3/14/08 

## 7:00 32 33 3/14/087:15 28 3/14/08 7:30 10.58 9.09 6.52 

## 5.59 28 3/14/08 7:45 28 3/14/08 8:00 

# 34 29 3/14/088:15 29 3/14/08 8:30 9.84 8.33 5.7./ 

## 4.78 29 3/14/08 8:45 31 3/14/08 9:00 32 30 3/14/089:15 28 3/14/08 9:30 10.84 9.65 6.38 

## 5.33 

# 34 3/14/08 9:45 30 3/14/0810:00 32 31 3/14/0810:15 33 3/14/0810:30 

## 11.27 8.88 6.66 

## 5.60 

# 34 3/14/0810:45 30 3/14/08 11:00 30 32 3/14/0811 :15 31 3/14/08 11:30 10.30 8.25 6.23 

## 5.36 30 3/14/08 11:45 33 3/14/08 18:00 28 30 3/14/0818:15 33 3/14/08 18:30 28 3/14/08 18:45 11.06 7.40 5.80 

## 4.32 25 3/14/08 19:00 27 28 3/14/0819:15 27 3/14/0819:30 27 3/14/08 19:45 

## 10.28 7.10 5.52 

## 4.20 27 3/14/08 20:00 27 27 3/17/0814:00 24 3/17/0814:15 

## 23 3/17/0814:30 

## 24 3/17/0814:45 

## 7.75 5.97 5.13 

## 4.67 23 3/17/0815:00 

## 22 23 3/17/0815:15 

## 21 3/17/08 15:30 

## 21 3/17/0815:45 

## 7.37 5.56 4.3i 

## 3.64 20 3/17/08 16:00 

## 22 21 3/17/0816:15 20 3/17/0816:30 16 3/17/08 16:45 6.57 5.03 3.i5 

## 2.98 15 • Individual slack houriy data does not coincide with "on the hour" emission unillotals • houriy data in italics is generated using interpolated S02 concentration data ArcelorMittal Mincora Mine Pellet Plant

Datemme 3/13/08 

## 21 :30 3/13/08 

## 21 :45 3/13/08 22:00 3/13/0822:15 3/13/08 22:30 3/13/08 22:45 3/13/08 23:00 3/13/08 23:15 3/13/08 23:30 3/13/08 23:45 3/14/08 0:00 3/14/08 0:15 3/14/08 0:30 3/14/080:45 3/14/08 

## 1 :00 3/14/081:15 3/14/08 

## 1 :30 3/14/08 

## 1 :45 3/14/082:00 3/14/08 2:15 3/14/08 2:30 3/14/08 2:45 3/14/08 3:00 3/14/083:15 3/14/08 3:30 3/14/08 3:45 3/14/084:00 3/14/084:15 3/14/084:30 3/14/084:45 3/14/08 5:00 3/14/08 5:15 3/14/08 5:30 3/14/08 5:45 3/14/08 6:00 3/14/086:15 3/14/08 6:30 3/14/086:45 3/14/08 

## 7:00 3/14/087:15 3/14/08 

## 7 :30 3/14/08 7:45 3/14/08 8:00 3/14/088:15 3/14/08 8:30 3/14/08 8:45 3/14/08 9:00 3/14/089:15 3/14/08 9:30 3/14/08 9:45 3/14/0810:00 3/14/0810:15 3/14/0810:30 3/14/0810:45 3/14/08 

## 11 :00 3/14/0811 :15 3/14/08 

## 11 :30 3/14/08 

## 11 :45 3/14/08 18:00 3/14/0818:15 3/14/08 18:30 3/14/08 18:45 3/14/08 19:00 3/14/0819:15 3/14/0819:30 3/14/08 19:45 3/14/08 20:00 3/17/0814:00 3/17/0814:15 3/17/0814:30 3/17/0814:45 3/17/0815:00 3/17/0815:15 3/17/08 15:30 3/1710815:45 3/17/08 16:00 3/17/0816:15 3/1710816:30 3/17/08 16:45 

## Stack A Hourly Average

Iblhr S02

6.22

6.59

9.10

10.16

6.94
6,43
8,43

9.02

8.92

10.14

10.58

9.84

10.84

11.27

10.30

11.06

10.28

7.75

7.37

6.57 Sulfur Dioxide Test Resutls Summary Furnace Line Waste Gas Stacks Stack 8 Stack C Stack D Hourly Average Hourly Average Hourly Average

Iblhr S02 IblhrS02 IblhrS02

5.29 3.9-1 

## 3.58

5.76 -1.12 

## 3.71

8.08 

## S.1i 4.23
9,43 5.89 

## 4.91

6.00 -1.21 

## 3.67

5.28 -1.0] 

## 3.61

7.25 4.97 

## 4.22

7.93 5.27 

## 4,40

8.11 

## 5.22 4,40

9.29 

## 6.20 5,41

9.09 6.5] 

## 5.59

8.33 5.7./ 

## 4.78

9.65 6.38 

## 5.33

8.88 6.66 

## 5.60

8.25 6.23 

## 5.36

7,40 

## 5.80 4.32

7.10 5.52 

## 4.20

5.97 

## 5.13 4.67

5.56 -1.37 

## 3.64

5.03 3. 

# is 2.98

• Individual stack hourly data does not coincide with "on the hour" emission unit totals
• hourly data in italics is generated using interpolated 502 concentration data 8arr Engineering Co. December 5, 2008

Total Emission Unit Total Emission Unit 15 minute average On the hour Iblhr S02 Iblhr 502

18 17 16 17 20 27 30 28 26 25 24 27 34 27 32 29 23 19 26 19 22 21 16 19 20 21 25 24 22 25 25 26 26 26 29 26 28 25 27 25 28 29 30 28 32 

# 34 36 32 33 28 28 28 

# 34 29 29 29 31 32 30 28 

# 34 30 32 31 33 

# 34 30 30 32 31 30 33 28 30 33 28 25 27 28 27 27 27 27 27 24 23 24 23 22 23 21 21 20 22 21 20 16 15

## ArcelorMittal Mincora Mine Pellet Plant Sulfur Dioxide Test Resutls Summary Furnace Line Waste Gas Stacks Barr Engineering Co. December 5, 2008
Stack A Stack B Stack C Stack D Total Emission Unit Total Emission Unit Hourly Average Hourly Average Hourly Average Hourly Average 15 minute average On the hour Datemme Iblhr S02 lblhr 502 Iblhr 502 Iblhr 502 IblhrS02 Iblhr 502 3/17/0817:00 17 17 3/17/0817:15 19 3/17/0817:30 22 3/17/0817:45 7.12 5.50**~.1I** 

## 3.27 22 3/17/0818:00 23 21 3/17/0818:15 24 3/17/0818:30 20 3/17/0818:45 7.93 6.20**~,4~** 

## 3.41 21 3/17/0819:00 20 21 3/17/0819:15 24 3/17/08 19:30 24 3/17/08 19:45 8.23 6.64**~.iO** 

## 3.68 25 3/17/08 20:00 21 24 3/17/0820:15 16 3/17/08 20:30 20 3/17/08 20:45 7.15 5.70 3.91 3.12 21 3/18/08 10:00 24 3/18/0810:15 32 3/18/08 10:30 31 3/18/08 10:45 9.37 7.75 6.22 

## 5.63 30 3/18/08 11:00 30 31 3/18/0811:15 31 3/18/08 11:30 30 3/18/08 11:45 10.02 7.58 6.3/ 5.58 27 3/18/08 12:00 30 29 3/18/0812:15 30 3/18/08 12:30 29 3/18/08 12:45 9.92 7.41 6.29 

## 5.76 28 3/18/08 13:00 26 28 3/18/0813:15 29 3/18/08 13:30 29 3/18/08 13:45 9.55 7.68 6.18 5.56 32 3/18/08 14:00 32 31 3/18/0814:15 32 3/18/08 14:30 30 3/18/08 14:45 9.72 8.19 6.6i 6.34 29 3/18/08 15:00 29 30 3/18/0815:15 30 3/18/08 15:30 32 3/18/08 15:45 9.83 8.19 6.M 6.22 33 3/18/08 16:00 33 32 3/18/0816:15 33 3/18/08 16:30 36 3/18/08 16:45 10.68 8.97 

# t.io 6.58 32 3/18/0817:00 34 34 3/18/0817:15 37 3/18/0817:30 38 3/18/0817:45 11.79 9.97 8.16 7.83 42 3/18/08 18:00 37 38 3/18/0818:15 37 3/18/08 18:30 41 3/18/08 18:45 12.13 10.45 8.8i 9.96 43 3/18/08 19:00 42 41 3/18/0819:15 40 3/18/08 19:30 43 3/18/08 19:45 11.98 10.21 9.N 9.47 39 3/18/08 20:00 42 41 3/1810820:15 42 3/1810820:30 39 3/18/08 20:45 11.66 10.06 9,42 9.82 40 3/18/08 21:00 35 39 3/18/0821 :15 34 3/18/0821:30 33 3/18/0821:45 10.21 8.52 6.96 6.44 27 3/18/08 22:00 26 30 3/18/08 22:15 24 3/1810822:30 24 3/18/08 22:45 8.58 6.76**5.()~** 

## 4.12 24 3/18/08 23:00 23 24 3/18/0823:15 21 3/18/08 23:30 23 3/18/08 23:45 7.62 6.33 -1.77 

## 4.16 24 3/19/08 0:00 26 24 3/19/080:15 23 3/19/08 0:30 18 3/19/08 0:45 6.97 5.45**~.23** 

## 3.53 14 3/19/08 1:00 13 17 3/19/081:15 15 • Individual stack hourly data does not coincide with "on the hour" emission unit totals • hourly data in italics is generated using interpolated 502 concentration data ArcelorMittal Mincora Mine Pellet Plant

Datemme 3/17/0817:00 3/17/0817:15 3/17/0817:30 3/17/0817:45 3/17/0818:00 3/17/0818:15 3/17/0818:30 3/17/0818:45 3/17/0819:00 3/17/0819:15 3/17/08 19:30 3/17/08 19:45 3/17108 20:00 3/17/0820:15 3/17/08 20:30 3/17108 20:45 3/18/08 

## 10:00 3/18/0810:15 3/18/08 

## 10:30 3/18/08 

## 10:45 3/18/08 

## 11 :00 3/18/0811:15 3/18/08 

## 11 :30 3/18/08 

## 11 :45 3/18/08 12:00 3/18/0812:15 3/18/08 12:30 3/18/08 12:45 3/18/08 13:00 3/18/0813:15 3/18/08 13:30 3/18/08 13:45 3/18/08 14:00 3/18/0814:15 3/18/08 14:30 3/18/08 14:45 3/18/08 15:00 3/18/0815:15 3/18/08 15:30 3/18/08 15:45 3/18/08 16:00 3/18/0816:15 3/18/08 16:30 3/18/08 16:45 3/18/0817:00 3/18/0817:15 3/18/0817:30 3/18/0817:45 3/18/08 18:00 3/18/0818:15 3/18/08 18:30 3/18/08 18:45 3/18/08 19:00 3/18/0819:15 3/18/08 19:30 3/18/08 19:45 3/18/08 20:00 3/18/0820:15 3/18/08 20:30 3/18/08 20:45 3/18/08 

## 21 :00 3/18/0821 :15 3/18/0821:30 3/18/0821:45 3/18/08 22:00 3/18/08 22:15 3/18/08 22:30 3/18/08 22:45 3/18/08 23:00 3/18/0823:15 3/18/08 23:30 3/18/08 23:45 3/19/08 0:00 3/19/080:15 3/19/08 0:30 3/19/08 0:45 3/19/08 

## 1 :00 3/19/081:15 

## Stack A Hourly Average

Iblhr S02

7.12

7.93

8.23

7.15

9.37

10.02

9.92

9.55

9.72

9.83

10.68

11.79

12.13

11.98

11.66

10.21

8.58

7.62

6.97 Sulfur Dioxide Test Resutis Summary Furnace Line Waste Gas Stacks Slack B Stack C Stack D Hourly Average Hourly Average Hourly Average

Iblhr S02 Iblhr S02 Iblhr S02

5.50**~.II** 

## 3.27

6.20**~,4~** 

## 3.41

6.64**~.70** 

## 3.68

5.70 3.91 

## 3.12

7.75 6.22 

## 5.63

7.58 6.31 

## 5.58

7.41 6.2Y 

## 5.76

7.68 6.18 

## 5.56

8.19 

## 6.67 6.34

8.19 6.M 

## 6.22

8.97 7.10 

## 6.58

9.97 

## 8./6 7.83

10.45 

## 8.87 9.96

10.21 9.N 

## 9.47

10.06 9,42 

## 9.82

8.52 6.96 

## 6.44

6.76 5.(N 

## 4.12

6.33 -1.77 

## 4.16

5.45**~.23** 

## 3.53

• Individual stack hourly data does not coincide with "on the hour" emission unit totals
• hourly data in italics is generated using interpolated S02 concentration data Barr Engineering Co. December 5, 2008

Total Emission Unit Total Emission Unit 15 minute average On the hour IblhrS02 Iblhr S02

17 17 19 22 22 23 21 24 20 21 20 21 24 24 25 21 24 16 20 21 24 32 31 30 30 31 31 30 27 30 29 30 29 28 26 28 29 29 32 32 31 32 30 29 29 30 30 32 33 33 32 33 36 32 34 34 37 38 42 37 38 37 41 43 42 41 

## 40 43 39 42 41 

## 42 39 40 35 39 34 33 27 26 30 24 24 24 23 24 21 23 24 26 24 23 18 14 13 17 15

## ArcelorMittal Mincora Mine Pellet Plant Sulfur Dioxide Test Resutls Summary Furnace Line Waste Gas Slacks Barr Engineering Co. December 5, 2008
Stack A Stack B Stack C Stack D Total Emission Unit Total Emission Unit Houriy Average Hourly Average Hourly Average Hourly Average 15 minute average On the hour Date/Time Iblhr S02 IblhrS02 Iblhr S02 Iblhr S02 Iblhr S02 Iblhr S02 3/19/08 1:30 11 3/19/08 1:45 4.78 3.58 2.61 1.92 13 3/19/08 2:00 13 13 3/19/082:15 12 3/19/08 2:30 11 3/19/08 2:45 4.77 2.66**2.~7** 

## 1.67 10 3/19/08 3:00 12 11 3/19/08 3:15 10 3/19/08 3:30 14 3/19/08 3:45 4.95 2.60 2.52 

## 1.66 11 3/19/08 4:00 12 12 3/19/084:15 13 3/19/08 4:30 10 3/19/08 4:45 4.68 2.14 2.-15 

## 1.66 9 3/19/08 5:00 10 10 3/19/085:15 12 3/19/08 5:30 12 3/19/08 5:45 5.00 1.69 2.65 

## 1.81 11 3/19/08 6:00 11 11 3/19/08 6:15 10 3/19/08 6:30 8 3/19/08 6:45 4.78 1.61 2.33 1.39 11 3/19/087:00 16 11 3/19/087:15 21 3/19/087:30 22 3/19/087:45 7.16 4.75**~.02** 

## 2.76 19 3/19/08 8:00 26 22 3/19/08 8:15 22 3/19/08 8:30 22 3/19/08 8:45 7.91 5.95**~.77** 

## 3.70 24 3/19/08 9:00 22 23 3/19/08 9:15 21 3/19/08 9:30 19 3/19/08 9:45 7.42 5.73**~.IO** 

## 3.57 20 3/19/0810:00 22 21 3/19/0810:15 25 3/19/08 10:30 26 3/19/08 10:45 8.49 6.82 

## 5./0 4.22 26 3/19/08 11:00 23 25 3/19/0811:15 23 3/19/08 11:30 22 3/19/0811:45 7.60 6.15 . .J. i-l 

## 4.06 22 3/19/08 12:00 24 23 3/19/0812:15 23 3/19/08 12:30 24 3/19/08 12:45 7.98 6.50**~.80** 

## 4.01 22 3/19/08 13:00 23 23 3/19/0813:15 24 3/19/08 13:30 25 3/19/08 13:45 8.37 6.84 5.20 

## 4.48 27 3/19/08 14:00 25 25 3/19/0814:15 25 3/19/0814:30 26 3/19/08 14:45 8.84 7.34 

## 5AI 4.60 28 3/19/08 15:00 27 27 3/19/0815:15 26 3/19/08 15:30 23 3/19/08 15:45 8.61 7.08 

## 5.05 4.28 24 3/19/08 16:00 25 24 3/19/0816:15 26 3/19/08 16:30 25 3/1910816:45 9.23 6.83 

## 5.10 4.40 27 311910817:00 26 26 3/19/0817:15 28 3/19/08 17:30 26 3/19/0817:45 9.39 6.72 5.20 

## 4.47 23 3/19/08 18:00 24 25 3/19/0818:15 26 3/19/08 18:30 27 3/19/08 18:45 9.61 7.10 

## 5.i2 4.98 33 3/19/08 19:00 38 31 3/19108 19:15 35 3/19/08 19:30 31 3/1910819:45 10.88 8.49 

## 7.06 6.60 29 3/19/08 20:00 29 31 3/19/0820:15 28 3/19/08 20:30 29 3/19/08 20:45 9.83 7.51 

## 6.03 5.32 29 3/19/0821:00 29 29 • Individual stack hourly data does not coincide with "on the hour" emission unit totals • hourly data in italics is generated using interpolated S02 concentration data ArcelorMiltal Mincora Mine Pellet Plant

Datemme 3/19/08 

## 1 :30 3/19/08 

## 1 :45 3/19/08 2:00 3/19/082:15 3/19/08 2:30 3/19/08 2:45 3/19/08 3:00 3/19/08 

## 3:15 3/19/08 3:30 3/19/08 3:45 3/19/08 4:00 3/19/084:15 3/19/08 4:30 3/19/08 4:45 3/19/08 5:00 3/19/085:15 3/19/08 5:30 3/19/08 5:45 3/19/08 6:00 3/19/08 6:15 3/19/08 6:30 3/19/08 6:45 3/19/087:00 3/19/087:15 3/19/087:30 3/19/087:45 3/19/08 8:00 3/19/08 8:15 3/19/08 8:30 3/19/08 8:45 3/19/08 9:00 3/19/08 9:15 3/19/08 9:30 3/19/08 9:45 3/19/0810:00 3/19/0810:15 3/19/08 

## 10:30 3/19/08 

## 10:45 3/19/08 

## 11 :00 3/19/0811:15 3/19/08 

## 11 :30 3/19/0811:45 3/19/08 12:00 3/19/0812:15 3/19/08 12:30 3/19/08 12:45 3/19/08 13:00 3/19/0813:15 3/19/08 13:30 3/19/08 13:45 3/19/08 14:00 3/19/0814:15 3/19/0814:30 3/19/08 14:45 3/19/08 15:00 3/19/0815:15 3/19/08 15:30 3/19/08 15:45 3/19/08 16:00 3/19/0816:15 3/19/08 16:30 3/19/08 16:45 3/19/0817:00 3/19/0817:15 3/19/08 17:30 3/19/0817:45 3/19/08 18:00 3/19/0818:15 3/19/08 18:30 3/19/08 18:45 3/19/08 19:00 3/19/08 

## 19:15 3/19/08 19:30 3/19/0819:45 3/19/08 20:00 3/19/0820:15 3/19/08 20:30 3/19/08 20:45 3/19/0821:00 

## Stack A Hourty Average

Iblhr S02

4.78

4.77

4.95

4.68

5.00

4.78

7.16

7.91

7.42

8.49

7.60

7.98

8.37

8.84

8.61

9.23

9.39

9.61

10.88

9.83 

## Sulfur Dioxide Test Resutls Summary Furnace Line Waste Gas Stacks Stack B Stack C Stack D Hourty Average Hourty Average Hourty Average

IblhrS02 Iblhr S02 Iblhr S02

3.58 

## 2.61 1.92

2.66**2.~7** 

## 1.67

2.60 2.52 

## 1.66

2.14 2..15 

## 1.66

1.69 2.65 

## 1.81

1.61 2.33 

## 1.39

4.75**~.02** 

## 2.76

5.95**~.i7** 

## 3.70

5.73**~.10** 

## 3.57

6.82 

## 5.10 4.22

6.15 . .J. i-l 

## 4.06

6.50**~.80** 

## 4.01

6.84 5.20 

## 4.48

7.34 

## 5AI 4.60

7.08 

## 5.05 4.28

6.83 

## 5.10 4.40

6.72 5.20 

## 4.47

7.10 

## 5.i2 4.98

8.49 

## 7.06 6.60

7.51 

## 6.03 5.32

• Individual stack hourty data does not coincide with "on the hour" emission unit totals
• hourty data in italics is generated using interpolated S02 concentration data Barr Engineering Co. December 5, 2008

Total Emission Unit Total Emission Unit 15 minute average On the hour Iblhr S02 Iblhr S02

11 13 13 13 12 11 10 12 11 10 14 11 12 12 13 10 9 10 10 12 12 11 11 11 10 8 11 16 11 21 22 19 26 22 22 22 24 22 23 21 19 20 22 21 25 26 26 23 25 23 22 22 24 23 23 24 22 23 23 24 25 27 25 25 25 26 28 27 27 26 23 24 25 24 26 25 27 26 26 28 26 23 24 25 26 27 33 38 31 35 31 29 29 31 28 29 29 29 29

## ArcelorMittal Mincora Mine Pellet Plant Sulfur Dioxide Test Resulls Summary Furnace Line Waste Gas Stacks Barr Engineering Co. December 5. 2008
Stack A Stack S Stack C Stack D Total Emission Unit Total Emission Unit Hourly Average Hourly Average Hourly Average Hourly Average 15 minute average On the hour Datemme Iblhr S02 IblhrS02 Iblhr S02 IblhrS02 Iblhr S02 Iblhr S02 3/19/0821:15 

## 28 3/19/0821 :30 

## 25 3/19/0821:45 

## 8.80 6.70 

## 5.52 5.04 23 3/19/08 22:00 

## 23 25 3/19/0822:15 

## 24 3/19/08 22:30 

## 23 3/19/08 22:45 

## 7.99 6.38 5.01 

## 4.49 26 3/19/08 23:00 

## 24 24 3/19/08 23:15 

## 25 3/19/08 23:30 

## 24 3/19/08 23:45 

## 8.06 6.24 -t.**7~** 

## 4.53 19 3/20108 0:00 

## 23 23 3/201080:15 

## 24 3/20108 0:30 

## 21 3/20108 0:45 

## 7.48 6.11**~.60** 

## 4.03 20 3/20108 

## 1:00 19 21 3/20108 

## 1:15 19 3/20108 

## 1:30 23 3/20108 

## 1:45 6.85 5.46**~.26** 

## 3.70 20 3/20108 2:00 

## 17 20 3/20108 2:15 

## 19 3/20108 2:30 

## 18 3/20108 2:45 

## 6.66 4.68**3.~6** 

## 2.56 15 3/20108 3:00 

## 18 18 3/201083:15 

## 20 3/20108 3:30 

## 21 3/20108 3:45 

## 7.69 4.98 -1.36 

## 3.55 23 3/20108 4:00 

## 25 22 3/201084:15 

## 27 3/20108 4:30 

## 30 3/20106 4:45 

## 9.79 7.18 6.18 

## 5.49 33 3/20108 5:00 

## 30 30 3/201085:15 

## 32 3/20108 5:30 

## 32 3/20108 5:45 

## 10.15 7.98 

## 6.25 5.55 26 3/20108 6:00 

## 26 29 3/201086:15 

## 28 3/20108 6:30 

## 26 3/20108 6:45 

## 9.16 7.14**5.3~** 

## 4.43 24 3/20108 7:00 

## 23 25 3/201087:15 

## 22 3/201087:30 

## 27 3/20108 

## 7:45 8.93 6.30**~.99** 

## 4.18 27 3/20108 8:00 

## 31 27 3/20108 8:15 

## 30 3/20108 8:30 

## 30 3/20108 8:45 

## 10.42 8.12 

## 6.42 5.16 32 3/20108 9:00 

## 33 31 3/201089:15 

## 35 3/20108 9:30 

## 32 3/20108 9:45 

## 11.57 8.66 7.09 

## 5.92 33 3/20108 

## 10:00 36 34 3/2010810:15 

## 37 3/20108 

## 10:30 32 3/20108 

## 10:45 11.45 8.61 i.J5 

## 6.04 28 3/20108 

## 11:00 32 32 3/20108 

## 11:15 37 3/20108 

## 11:30 44 3/20108 

## 11:45 12.75 9.82 

## 8.28 7.37 41 3/20108 12:00 

## 40 40 3/2010812:15 

## 44 3/20108 12:30 

## 45 3/20108 12:45 

## 14.51 11.69 

## 8.92 8.27 44 3/20108 13:00 

## 41 43 3/2010813:15 

## 43 3/20108 13:30 

## 43 3/20108 13:45 

## 14.66 12.01 

## 8.28 7.80 

## 44 312010814:00 

## 26 39 3/20108 14:15 

## 43 3120108 14:30 43 3/20108 14:45 

## 12.93 10.83 

## 7.82 8.74 36 3120108 15:00 35 39 312010815:15 

## 38 3/20108 15:30 

## 46 3/20108 15:45 

## 12.83 11.22 

## 7.85 8.41 42 3/20108 16:00 

## 42 42 3/20108 16:15 

## 40 3/20108 16:30 

## 42 3120108 16:45 

## 12.29 11.94 

## 8.11 9.04 41 • Individual stack hourly data does not coincide with "on the hour" emission unit totals • hourly data in italics is generated using interpolated S02 concentration data ArcelorMiltal Mincora Mine Pellet Plant

Datemme 3/19/0821:15 3/19/0821 :30 3/19/0821:45 3/19/08 22:00 3/19/0822:15 3/19/08 22:30 3/19/08 22:45 3/19108 23:00 3/19/08 23:15 3/19108 23:30 3/19/08 23:45 3/20108 0:00 

## 31201080:15 3/20108 0:30 3120108 0:45 3/20108 

## 1 :00 3/20108 

## 1 :15 3/20108 

## 1 :30 3/20108 

## 1 :45 3/20108 2:00 3/20108 2:15 3/20108 2:30 3/20108 2:45 3120108 3:00 3/201083:15 3/20108 3:30 3/20108 3:45 3/20108 4:00 3/201084:15 3/20108 4:30 3/20108 4:45 3/20108 5:00 3/201085:15 3/20108 5:30 3/20108 5:45 3/20108 6:00 3/201086:15 3/20108 6:30 3/20108 6:45 3/20108 7:00 3/201087:15 3/201087:30 3/20108 

## 7 :45 3/20108 8:00 3/20108 8:15 3/20108 8:30 3/20108 8:45 3/20108 9:00 3/201089:15 3/20108 9:30 3/20108 9:45 3/20108 

## 10:00 3/2010810:15 3/20108 

## 10:30 3/20108 

## 10:45 3/20108 

## 11 :00 3/20108 

## 11 :15 3/20108 

## 11 :30 3120108 

## 11 :45 3/20108 12:00 3/2010812:15 3/20108 12:30 3/20108 12:45 3/20108 13:00 3/2010813:15 3/20108 13:30 3/20108 13:45 3/2010814:00 3/20108 14:15 3/20108 14:30 3/20108 14:45 3/20108 15:00 3/2010815:15 3/20108 15:30 3/20108 15:45 3/20108 16:00 3/20108 16:15 3/20108 16:30 3/20108 16:45 

## Stack A Hourly Average

Iblhr S02

8.80

7.99

8.06

7.48

6.85

6.66

7.69

9.79

10.15

9.16

8.93

10.42

11.57

11.45

12.75

14.51

14.66

12.93

12.83

12.29 Sulfur Dioxide Test Resutls Summary Furnace Line Waste Gas Stacks Stack S Stack C Stack D Hourly Average Hourly Average Hourly Average

IblhrS02 tblhr S02 IblhrS02

6.70 

## 5.52 5.04

6.38 5.01 

## 4.49

6.24**~. 7~**  

## 4.53

6.11**~.60** 

## 4.03

5.46**~.26** 

## 3.70

4.68**3.~6** 

## 2.56

4.98 -1.36 

## 3.55

7.18 6.18 5.49

7.98 6.25 5.55

7.14**5.3~** 

## 4.43

6.30**~.99** 

## 4.18

8.12**6.~2** 

## 5.16

8.66 7.09 

## 5.92

8.61 i.J5 

## 6.04

9.82 8.28 7.37

11.69 8.92 8.27

12.01 

## 8.28 7.80

10.83 

## 7.82 8.74

11.22 7.85 8.41

11.94 8.11 9.04

• Individual stack hourly data does not coincide with "on the hour" emission unit totals
• hourly data in italics is generated using interpolated S02 concentration data Sarr Engineering Co. December 5, 2008

Total Emission Unit Total Emission Unit 15 minute average On the hour Iblhr S02 Iblhr S02

28 25 23 23 25 24 23 26 24 24 25 24 19 23 23 24 21 20 19 21 19 23 20 17 20 19 18 15 18 18 20 21 23 25 22 27 30 33 30 30 32 32 26 26 29 28 26 24 23 25 22 27 27 31 27 30 30 32 33 31 35 32 33 36 34 37 32 28 32 32 37 44 41 40 40 44 45 44 41 43 43 43 

## 44 26 39 43 43 36 35 39 38 46 42 42 42 40 42 41

## ArcelorMittal Mincora Mine Pellet Plant Sutfur Dioxide Test Resutls Summary Furnace Line Waste Gas Stacks Barr Engineering Co. December 5, 2008
Stack A Stack B Stack C Slack D Total Emission Unit Total Emission Unit Hourty Average Hourty Average Hourty Average Hourty Average 15 minute average On the hour Date/Time 

## Iblhr S02 IblhrS02 Iblhr S02 Iblhr S02 Iblhr S02 Iblhr S02 3/20/08 17:00 36 40 3/20/0817:15 33 3/20/08 17:30 27 3/20/0817:45 9.86 9.i0 

## 6.62 7.45 32 3/20/08 18:00 31 31 3/20/0818:15 31 3/20/08 18:30 32 3/20/08 18:45 9.78 9.38 6.05 6.82 33 3/20/08 19:00 35 32 3/20/0819:15 31 3/20/08 19:30 25 3/20/08 19:45 10.40 8.37 6.06 5.70 29 3/20/08 20:00 29 28 3/20/08 20:15 28 3/20/08 20:30 28 3/20/08 20:45 9.36 7.96 6.15 5.22 30 3/20/08 21:00 33 30 3/20/0821:15 30 3/20/0821:30 34 3/20/0821 :45 11.10 9.06 

## 7.20 5.91 36 3/20/08 22:00 34 

## 34 3/20/0822:15 34 

## 3120/08 22:30 33 3/20/08 22:45 10.69 8.33 6.71 5.72 25 3/20/08 23:00 23 29 3/20/08 23:15 21 3/20/08 23:30 18 3/20/08 23:45 7.71 5.-16 

## 4.30 3.30 21 3/21/080:00 26 21 3/21/080:15 24 3/21/080:30 26 3/21/080:45 9.15 6.56 5.45 4.08 26 3/21/081:00 28 26 3/21/081:15 26 3/21/08 1:30 29 3/21/08 1:45 9.67 i.56 

## 6.23 4.77 30 3/21/082:00 29 29 3/21/082:15 29 3/21/082:30 25 3/21/082:45 9.67 7.-10 

## 6.14 4.60 27 3/21/083:00 28 27 3/21/08 3:15 30 3/21/083:30 28 3/21/083:45 9.63 7.6-1 

## 6.35 4.96 29 3/21/08 4:00 29 29 3/21/084:15 27 3/21/084:30 25 3/21/084:45 9.16 6.68 5.64 4.20 22 3/21/085:00 24 24 3/21/085:15 30 3/21/085:30 35 3/21/085:45 9.80 8.20 

## 7.11 5.67 35 3/21/086:00 32 33 3/21/086:15 32 3/21/086:30 30 3/21/086:45 10.14 8.2-1 

## 6.84 5.37 28 3/21/087:00 27 29 3/21/087:15 30 3/21/087:30 29 3/21/08 7:45 9.58 7.-1/ 

## 6.04 4.43 24 3/21/08 8:00 21 26 3/21/088:15 26 3/21/088:30 30 3/21/088:45 9.17 i.05 

## 5.81 4.46 32 3/21/089:00 32 30 3/21/089:15 25 3/21/08 9:30 23 3/21/089:45 9.04 6.32 

## 5.32 3.62 23 3/21/0810:00 18 22 3/21/0810:15 21 

## 3121/0810:30 19 3/21/0810:45 7.39 5.00 

## 4.06 2.93 18 3/21/08 11:00 18 19 3/21/0811:15 18 3/21/08 11:30 20 3/21/08 11:45 7.24 5.-13 

## 3.89 3.23 23 3/21/08 12:00 22 21 3/21/0812:15 20 3/21/0812:30 19 • Individual stack hourty data does not coincide with "on the hour" emission unit totals • hourty data in italics is generated using interpolated S02 concentration data ArcelorMittal Mincora Mine Pellet Plant

Datemme 3/20108 17:00 3/2010817:15 3/20108 

## 17 :30 3/2010817:45 3120108 18:00 3/2010818:15 3120108 18:30 

## 3120108 18:45 3120108 19:00 

## 312010819:15 3120108 19:30 3/20108 19:45 3/20108 20:00 3120108 20:15 3/20108 20:30 3/20108 20:45 3/20108 

## 21 :00 3/2010821:15 3/2010821:30 

## 312010821 :45 3120108 22:00 

## 312010822:15 3120108 22:30 

## 3120108 22:45 3120108 23:00 3120108 23:15 3/20108 23:30 3/20108 23:45 3/21/080:00 3/21/080:15 3121/080:30 3121/080:45 3121/081:00 3121/081:15 3121108 

## 1 :30 3121108 1 :45 3/211082:00 3121/082:15 3121/082:30 3121/082:45 3121/083:00 

## 3121108 3:15 31211083:30 31211083:45 3121108 4:00 

## 31211084:15 31211084:30 31211084:45 3/211085:00 

## 31211085:15 3/21/085:30 3/21/085:45 3121/086:00 3121/086:15 3121/086:30 3121/086:45 3121/087:00 3121/087:15 

## 31211087:30 3121108 7:45 3121108 8:00 31211088:15 

## 31211088:30 3/211088:45 3/211089:00 3/211089:15 3121/08 

## 9 :30 3121/089:45 3121/0810:00 

## 312110810:15 312110810:30 3/2110810:45 3121108 

## 11 :00 3/2110811:15 3/21108 

## 11 :30 3121/08 

## 11 :45 3121/08 12:00 3121/0812:15 

## 312110812:30 Stack A Hourly Average

Iblhr S02

9.86

9.78

10.40

9.36

11.10



## 10.69

7.71

9.15

9.67

9.67

9.63

9.16

9.80

10.14

9.58

9.17

9.04

7.39

7.24 Sulfur Dioxide Test Resutls Summary Furnace Line Waste Gas Stacks Stack B Stack C Stack D Hourly Average Hourly Average Hourly Average

IblhrS02 Iblhr S02 Iblhr S02

9.i0 

## 6.62 7.45



## 9.38 6.05 6.82



## 8.37 6.06 5.70



## 7.96 6.15 5.22

9.06 

## 7.20 5.91



## 8.33 6.71 5.72



## 5..16 4.30 3.30



## 6.56 5.45 4.08

i.56 

## 6.23 4.77**7.~0** 

## 6.14 4.60

7.64 

## 6.35 4.96



## 6.68 5.64 4.20



## 8.20 

## 7.11 5.67**8.2~** 

## 6.84 5.37

7..11 6.04 

## 4.43

i.05 

## 5.81 4.46

6.32 

## 5.32 3.62

5.00 

## 4.06 2.93**5.~3** 

## 3.89 3.23

• Individual stack hourly data does not coincide with "on the hour" emission unit totals
• hourly data in italics is generated using interpolated S02 concentration data Barr Engineering Co. December 5, 2008

Tolal Emission Unit Total Emission Unit 15 minute average On the hour Iblhr S02 Iblhr S02

36 40 33 27 32 31 31 31 32 33 35 32 31 25 29 29 28 28 28 30 33 30 30 34 36 34 

## 34 34 33 25 23 29 21 18 21 26 21 24 26 26 28 26 26 29 30 29 29 29 25 27 28 27 30 28 29 29 29 27 25 22 24 24 30 35 35 32 33 32 30 28 27 29 30 29 24 21 26 26 30 32 32 30 25 23 23 18 22 21 19 18 18 19 18 20 23 22 21 20 19

## ArcelorMittal Mincora Mine Pellet Plant Sulfur Dioxide Test Resutls Summary Furnace Line Waste Gas Stacks Barr Engineering Co. December 5, 2008
Stack A Stack B Stack C Stack D Total Emission Unit Total Emission Unit Hourly Average Hourly Average Hourly Average Hourly Average 15 minute average On the hour Datemme Iblhr S02 Iblhr S02 Iblhr S02 Ib/hr S02 Iblhr S02 Iblhr S02 3/21108 12:45 

## 7.47 

## 5.46 3.93 3.26 19 3/21/0813:00 

## 19 19 3/21/0813:15 

## 19 3/21/0813:30 

## 23 3/21/08 13:45 

## 8.22 

## 5.82 4.21 3.46 25 3/21/08 14:00 

## 24 23 3/21/08 14:15 

## 22 3/21/0814:30 

## 22 3/21/0814:45 

## 8.04 6.10 

## 4.46 3.73 21 3/21/0815:00 

## 19 21 3/21/0815:15 

## 21 3/21/0815:30 

## 21 3/21/08 15:45 

## 7.45 

## 5.69 4.08 3.52 21 3/21/08 16:00 

## 23 22 3/21/0816:15 

## 22 3/21/0816:30 

## 18 3/21/08 16:45 

## 7.14 5.40 

## 3.77 3.28 16 3/21108 17:00 

## 17 18 3/21/0817:15 

## 19 3/21/08 17:30 

## 22 3/21/08 17:45 

## 7.48 5.52 

## 3.90 3.30 22 3/21/08 18:00 

## 22 21 3/21/0818:15 

## 23 3/21/0818:30 

## 27 3/21108 18:45 

## 8.95 

## 6.69 5.12 4.19 28 3/21/0819:00 

## 30 27 3/21/0819:15 

## 30 3/21/0819:30 

## 28 3/21/08 19:45 

## 10.19 

## 7.68 5.81 4.85 26 3/21/08 20:00 

## 25 27 3/21108 

## 20:15 31 3/21/0820:30 

## 33 3/2110820:45 

## 10.38 8.20 

## 6.19 5.34 32 3/21/0821 :00 

## 33 32 3/21/0821:15 

## 30 3/21/0821:30 

## 29 3/21/08 

## 21:45 10.47 

## 8.37 6.10 5.59 30 3/21/08 22:00 

## 29 30 3/21/0822:15 

## 30 3/21/0822:30 

## 28 3/21/0822:45 

## 10.12 

# r.rs 5.75 5.31 28 3/21/0823:00 

## 29 29 3/21/0823:15 

## 27 3/21/08 23:30 

## 25 3/21/08 23:45 

## 9.57 

## 7.28 5.34 4.57 25 3/22108 0:00 

## 26 26 3/221080:15 

## 30 3/22108 0:30 

## 31 3/22108 0:45 

## 9.41 

## 7.97 5.98 5.35 28 3/22108 

## 1:00 29 29 3/22108 

## 1:15 30 3/22108 

## 1:30 28 3/22108 

## 1:45 9.05 8.ll 

## 6.18 5.94 29 3/22108 2:00 

## 30 29 3/221082:15 

## 30 3/22108 2:30 

## 32 3/22108 2:45 

## 9.48 

## 8.91 6.25 6.34 32 3/22108 3:00 

## 30 31 3/22108 

## 3:15 25 3/221083:30 

## 22 3/22108 3:45 

## 8.37 7.03 

## 4.99 4.58 23 3/22108 4:00 

## 23 23 3/221084:15 

## 27 3/22108 4:30 

## 24 3/22108 4:45 

## 8.00 

## 6.58 4.84 4.37 22 3/22108 5:00 

## 22 24 3/22108 

## 5:15 25 3/22108 5:30 

## 26 3/22108 5:45 

## 8.69 

## 6.48 4.85 4.26 24 3/22108 6:00 

## 22 24 3/22108 6:15 

## 23 3/22108 6:30 

## 25 3/22108 6:45 

## 8.59 

## 6.44 4.80 4.25 27 3/22108 7:00 

## 31 26 3/22108 

## 7:15 30 3/22108 7:30 

## 27 3/22108 7:45 

## 10.05 7.92 

## 6.01 5.77 29 3/22108 

## 8:00 35 30

Averaae 8.9 7.0 5.3 4.6 25.7 25.7 • Individual stack hourly data does not coincide with "on the hour" emission unit totals • hourly data in italics is generated using interpolated 502 concentration data 

## ArcelorMittal Mincora Mine Pellet Plant

Datemme 3/21108 12:45 3/21/0813:00 3/21/0813:15 3/21/0813:30 3/21/08 13:45 3/21/08 14:00 3/21/08 14:15 3/21/0814:30 3/21/0814:45 3/21/0815:00 3/21/0815:15 3/21/0815:30 3/21/08 15:45 3/21/08 16:00 3/21/0816:15 3/21/0816:30 3/21/08 16:45 3/21/08 17:00 3/21/0817:15 3/21/08 17:30 3/21/08 17:45 3/21/08 18:00 3/21/0818:15 3/21/0818:30 3/21/08 18:45 3/21/0819:00 3/21/0819:15 3/21/0819:30 3/21/08 19:45 3/21/08 20:00 3/21108 

## 20: 15 3/21/0820:30 3/21/0820:45 3/21/0821 :00 3/21/0821:15 3/21/0821:30 3/21/08 

## 21 :45 3/21/08 22:00 3/21/0822:15 3/21/0822:30 3/21/0822:45 3/21/0823:00 3/21/0823:15 3/21/08 23:30 3/21/08 23:45 3/22108 0:00 3/221080:15 3/22108 0:30 3/22108 0:45 3/22108 

## 1:00 3/22108 

## 1:15 3/22108 

## 1:30 3/22108 

## 1 :45 3/22108 2:00 3/221082:15 3/22108 2:30 3/22108 2:45 3/22108 3:00 3/22108 

## 3: 15 3/221083:30 3/22108 3:45 3/22108 4:00 3/221084:15 3/22108 4:30 3/22108 4:45 3/22108 5:00 3/22108 

## 5: 15 3/22108 5:30 3/22108 5:45 3/22108 6:00 3/22108 6:15 3/22108 6:30 3/22108 6:45 3/22108 7:00 3/22108 

## 7: 15 3/22108 7:30 3/22108 7:45 3/22108 

## 8 :00

Averaqe Stack A Hourly Average

Iblhr S02

7.47

8.22

8.04

7.45

7.14

7.48

8.95

10.19

10.38

10.47

10.12

9.57

9.41

9.05

9.48

8.37

8.00

8.69

8.59

10.05 8.9 Sulfur Dioxide Test Resutls Summary Furnace Line Waste Gas Stacks Stack B Stack C Stack D Hourly Average Hourly Average Hourly Average

Iblhr S02 Iblhr S02 Ib/hr S02



## 5.46 3.93 3.26



## 5.82 4.21 3.46



## 6.10 4.46 3.73



## 5.69 4.08 3.52



## 5.40 3.77 3.28

5.52 

## 3.90 3.30



## 6.69 5.12 4.19



## 7.68 5.81 4.85

8.20 

## 6.19 5.34



## 8.37 6.10 5.59

i.75 

## 5.75 5.31



## 7.28 5.34 4.57



## 7.97 5.98 5.35

8.ll 

## 6.18 5.94



## 8.91 6.25 6.34



## 7.03 4.99 4.58



## 6.58 4.84 4.37



## 6.48 4.85 4.26



## 6.·/-1 4.80 4.25

7.92 

## 6.01 5.77 7.0 5.3 4.6 • Individual stack hourly data does not coincide with "on the hour" emission unit totals
• hourly data in italics is generated using interpolated S02 concentration data Barr Engineering Co. December 5, 2008
Total Emission Unit Total Emission Unit 15 minute average On the hour Iblhr S02 Iblhr S02 19 19 19 19 23 25 24 23 22 22 21 19 21 21 21 21 23 22 22 18 16 17 18 19 22 22 22 21 23 27 28 30 27 30 28 26 25 27 31 33 32 33 32 30 29 30 29 30 30 28 28 29 29 27 25 25 26 26 30 31 28 29 29 30 28 29 30 29 30 32 32 30 31 25 22 23 23 23 27 24 22 22 24 25 26 24 22 24 23 25 27 31 26 30 27 29 35 30 25.7 25.7

# ArcelorMittal Mincora Mine Pellet Plant Replacement S02 Values Stacks Band C 

# TIME STAMP 

# STACK A STACK B STACKC STACK D Results Results Results Results 

# replacemen replacemen 15 min interval S02AVerage S02Average S02 Average ppm 

# Dry ppm Dry ppm Dry

Ava Ava Avg Measured Mean 5.6 4.5 3.6 2.7 Mean incl Repl Values 5.6 4.6 3.4 2.7 

# 3/11/08 23:45 5.8 

# 3/12108 0:00 L 

# 3/121080:15 3/12108 0:30 3/121080:45 3/12108 1:00 

# 3/121081:15 3/12108 1:30 

# 4.2 

# 3/121081:45 

# r.E 4.7 

# 3/121082:00 7.4 

# 3/12108 2:15 

# 3/12108 2:30 3/12108 2:45 3/12108 3:00 3/121083:15 3/12108 3:30 3/12108 3:45 3/12108 4:00 3/121084:15 3/121084:30 3/12108 4:45 3/12108 5:00 3/12/085:15 3/12108 5:30 3/12108 5:45 .2 

# 3/12108 6:00 3/121086:15 3/121086:30 -_. 

# 3/12108 6:45 3/12108 7:00 3/12/087:15 3/12108 7:30 3/12108 7:45 3/12108 8:00 3/121088:15 5.1 

# 3/12108 8:30 5.9 

# 3/12108 8:45 6.7 

# 3/121089:00 6.2 

# 3/121089:15 3/12108 9:30 3/12108 9:45 3/12108 10:00 

# 3/1210810:15 3/1210810:30 3/12108 10:45 

# 3/12108 11:00 2 

# 3/1210811:15 2 

# 3/12108 11:30 

# 3/12108 11:45 2 

# 3/12108 12:00 

# 3/1210812:15 L 

# 3/12108 12:30 3/12108 12:45 3/1210813:00 3/1210813:15 3/12108 13:30 .4 

# 3/1210813:45 3 

# 3/1210& 14:00 3/1210814:15 3/12108 14:30 3/12108 14:45 Barr Engineering Co. December 5, 2008

* 

# note some replacement values are affected by Stack A or D calibration data. These results are not used in subsequent Ibllhr calculations ArcelorMittal Mincora Mine Pellet Plant 

# TIME STAMP

15 min interval Measured Mean Mean incl Repl Values 

# 3/11/08 23:45 3/12108 0:00 3/121080:15 3/12108 0:30 3/121080:45 3/12108 1:00 

# 3/121081:15 3/12108 1:30 

# 3/121081:45 3/121082:00 3/12108 2: 15 

# 3/12108 2:30 3/12108 2:45 3/12108 3:00 3/121083:15 3/12108 3:30 3/12108 3:45 3/12108 4:00 3/121084:15 3/121084:30 3/12108 4:45 3/12108 5:00 3/12/085:15 3/12108 5:30 3/12108 5:45 3/12108 6:00 3/121086:15 3/121086:30 3/12108 6:45 3/12108 7:00 3/12/087:15 3112108 7:30 3/12108 7:45 3/12108 8:00 3/121088:15 3/12108 8:30 3/12108 8:45 3/121089:00 3/121089:15 3/12108 9:30 3/12108 9:45 3/12108 10:00 

# 3/1210810:15 3/1210810:30 3/12108 10:45 

# 3/12108 11 :00 

# 3/1210811:15 3/12108 11 :30 

# 3/12108 11:45 

# 3/12108 12: 00 

# 3/1210812:15 3/12108 12:30 3/12108 12:45 3/1210813:00 3/1210813:15 3/12108 13:30 3/1210813:45 3/12101) 14:00 3/1210814:15 3/12108 14:30 3/12108 14:45 Replacement S02 Values Stacks Band C 

# STACK A STACK B Results Results 

# replacemen S02Average S02Average

ppm Dry ppm Dry

Avg AVQ 5.6 4.5 5.6 4.6 5.8 5.0 6.4 5.4 5.0 4.3 5.3 4.5 7.0 6.2 6.7 5.8 7.4 6.6 7.1 6.1 7.6 6.6 7.4 6.4 6.9 6.0 6.2 5.2 5.6 4.7 4.9 4.2 3.9 3.4 3.8 3.3 4.4 3.9 4.7 4.0 4.0 3.5 4.3 3.9 6.2 5.4 6.4 5.5 5.4 4.7 4.9 4.4 5.4 4.7 6.0 5.2 6.9 6.1 6.7 5.8 6.9 6.0 7.2 6.4 7.6 6.8 7.6 6.9 8.0 7.0 6.6 5.9 5.1 4.5 5.9 5.3 6.7 5.8 6.2 5.3 6.0 5.2 5.9 5.1 4.5 3.9 3.4 3.1 3.4 3.1 3.0 2.8 4.6 4.0 4.9 4.2 3.7 3.4 3.1 2.9 3.3 3.2 4.7 3.8 4.6 3.3 3.3 4.2 3.6 2.8 3.8 3.0 4.8 3.6 3.8 3.0 3.8 2.9 4.6 3.5 5.1 3.9 5.0 4.0 3.5 2.8 Barr Engineering Co. December 5, 2008 

# STACKC STACK D Results Results 

# replacemen 802 Average 802 Average

ppm Dry ppm Dry

--- 

# AVo. Avg 3.6 2.7 3.4 2.7 

# 3.1 2.2 

# 3.5 2.5 3.0 

# 2.4 

# 3.1 2.3 

# 3.8 2.7 

# 3.8 2.8 -1.2 

# 3.1 -1.2 

# 3.2 -1.7 

# 3.8 -1.-1 

# 3.5 -1.0 

# 3.1 

# 3.7 2.8 3.-1 

# 2.6 

# 3.1 2.5 

# 2.6 2.3 

# 2.6 2.3 

# 2.8 2.4 

# 2.9 2.3 

# 2.6 2.2 

# 2.8 2.3 

# 3.6 2.7 

# 3.6 2.6 

# 3.2

# .~.:.4- 2.9 .--

# ~~~=1=F~-= 3.2 3.-1

# -.-~i- 

# .. - 3.9 3.8 2.8 

# 3.8 2.7 -1.1 

# 3.1 -1.-1 

# 3.4 -1.5 

# 3.5 -1.5 

# 3.2 

# 3.6 2.5 3.0 

# 2.3 

# 3.3 2.4 

# 3.6 2.5 

# 3.3 2.3 

# 3.2 2.3 

# 3.2 2.3 

# 2.7 2.1 

# 2.3 2.0 

# 2.3 2.0 

# 2.1 1.9 

# 2.7 2.1 

# 2.9 2.2 

# 2.5 2.1 

# 2.2 2.0 

# 2.3 2.0 

# 2.8 2.2 

# 2.8 2.2 

# 2.2 1.9 

# 2.3 2.0 

# 3.9 4.4 

# 2.7 2.1 2.-1 

# 1.9 

# 2.3 1.8 

# 2.6 2.0 

# 2.8 2.0 

# 2.7 2.0 2.0 

# 1.5

* 

# note some replacement values are affected by Stack A or D calibration data. These results are not used in subsequent Ibl/hr calculations

# ArcelorMittal Mincora Mine Pellet Plant Replacement S02 Values Stacks Band C 

# TIMESTAMP 

# STACK A STACK B STACKC STACK D Results Results Results Results replacemen replacemen ·.···S02A"erage··· S02 Average S02Average 15 min interval 

# oPmOrY ppm Dry ppm Dry Avg Avg J 

# 3/1210815:00 3.2 

# 3/1210815:15 2.9 

# 3/1210815:30 3/1210815:45 3/1210816:00 3/1210816:15 3/12108 16:30 3/12108 16:45 3/12108 17:00 3/1210817:15 3/12108 23:45 7.4 

# -1.3 

# 3/13/08 0:00 6.6 3.7 3/13/080:15 8.2 -I. 

# 3/13/08 0:30 7.4 

# 3/13/08 0:45 7.8 

# 3/13/081:00 6.3 3/13/081:15 3/13/08 1:30 3/13/08 1:45 

# 3/13/08 2:00 3/13/082:15 3/13/08 2:30 3/13/08 2:45 3/13/08 3:00 -I. 

# 3/13/083:15 -1./ 3/13/08 3:30 -I. 

# 3/13/08 3:45 3/13/08 4:00 

# 3/13/084:15 3/13/08 4:30 3/13/08 4:45 3/13/08 5:00 

# 3/13/085:15 3/13/08 5:30

. 

# 3/13/08 5:45 -I.

.. 

## - ........ 

# 3/13/08 6:00 

# 5. 3/13/086:15 

# 5. .0_ ·0·' 

# 3/13/08 6:30 3/13/08 6:45 

# 3/13/08 7:00 3/13/087:15 

# 3/13/087:30 3/13/08 7:45 3/13/08 8:00 4.6 3/13/088:15 5.2 3/13/08 8:30 5.7 :.-/ 

# 3/13/08 8:45 

# :.6 3/13/08 9:00 

# .6 3/13/089:15 

# -1.0 3/13/08 9:30 3., 3/13/08 9:45 3/13/08 10:00 

# 3/13/0810:15 3/13/08 10:30 3/13/08 10:45 3/13/08 11:00 

# 3/13/0811:15 '.1 

# 3/13/08 11:30 3/13/08 11:45 

# '.0 3/13/08 12:00 4.5 3/13/0812:15 3.9 3/13/0812:30 2.7 3/13/08 12:45 1.7 Barr Engineering Co. December 5, 2008

• note some replacement values are affected by Stack A or D calibration data. These results are not used in subsequent Ibllhr calculations ArcelorMittal Mincora Mine Pellet Plant 

# TIMESTAMP

15 min interval 3/1210815:00 3/1210815:15 3/1210815:30 3/1210815:45 3/1210816:00 3/1210816:15 3/12108 16:30 3/12108 16:45 3/12108 17:00 3/1210817:15 3/12108 23:45 3/13/08 0:00 3/13/080:15 3/13/08 0:30 3/13/08 0:45 3/13/081:00 3/13/081:15 3/13/08 1:30 3/13/08 1:45 3/13/08 2:00 3/13/082:15 3/13/08 2:30 3/13/08 2:45 3/13/08 3:00 3/13/083:15 3/13/08 3:30 3/13/08 3:45 3/13/08 4:00 3/13/084:15 3/13/08 4:30 3113/08 4:45 3/13/08 5:00 3/13/085:15 3/13/08 5:30

- 

# 3/13/08 5:45 3/13/08 6:00 3/13/086:15 3/13/08 6:30 3/13/08 6:45 3/13/08 7:00 3/13/087:15 3/13/087:30 3/13/08 7:45 3/13/08 8:00 3/13/088:15 3/13/08 8:30 3/13/08 8:45 3/13/08 9:00 3/13/089:15 3/13/08 9:30 3/13/08 9:45 3/13/08 10:00 3/13/0810:15 3/13/08 10:30 3/13/08 10:45 3/13/08 11 :00 3/13/0811:15 3/13/08 11 :30 3/13/08 11:45 3/13/08 12:00 3/13/0812:15 3/13/0812:30 3/13/08 12:45 Replacement S02 Values Stacks Band C 

# STACK A STACK B Results Results replacemen S02Average S02 Average

ppm Dry ppm Dry

Avg Avg 3.2 2.6 2.9 2.6 3.4 2.9 2.7 2.5 2.6 2.5 2.9 2.6 3.5 3.1 3.9 3.3 4.5 3.7 4.8 3.9 7.4 6.2 6.6 5.3 8.2 6.4 7.4 6.0 7.8 6.2 6.3 5.0 6.1 4.8 7.1 5.6 6.9 5.4 6.3 4.9 6.5 5.1 7.2 5.8 7.3 5.9 7.7 6.2 7.8 6.3 7.5 6.1 7.9 6.4 6.5 5.2 6.4 4.9 6.7 5.1 6.4 5.1 6.3 5.1 6.6 5.6 6.7 5.8 7.4 6.7

.. 

# ·H- 1--

# +~ 6.9 6.3 6.8 6.2 6.9 6.2 6.4 5.7 5.5 4.3 4.1 3.4 4.6 3.7 5.2 3.9 5.7 4.4 5.9 4.4 5.9 4.6 6.6 5.0 5.9 4.7 5.8 4.5 5.6 4.3 6.0 4.7 5.8 4.7 6.1 5.4 4.5 4.4 4.3 3.3 5.0 4.1 5.2 4.2 4.5 3.9 3.9 3.3 2.7 2.4 1.7 1.7 Barr Engineering Co. December 5, 2008 

# STACKC STACK D Results Results replacemen .S02.Av9rage S02Average •. ··ppmDry
... ···.**~mDry** 

# Avg· Avg 1.8 

# J..i 

# j·B L5 2.1 1.7 

# 1.9 1.7 

# 1.8 1.7 

# 1.9 1.7 

# II 1.7 

# 2.3 1.8 

# 2.6 1.9 

# II 2.0 -1.3 

# 3.3 

# 3.7 2.8 -1.6 

# 3.4 -1.2 

# 3.1 -1.3 

# 3.1 

# 3.6 2.7 

# 3,5 2.6 -1.0 

# 2.9 

# 3.9 2.8 

# 3.5 2.6 

# 3.6 2.7 -1.1 

# 3.1 -1.3 

# 3.3 -1.6

# ~ -1.6 

# 3.5 -1.5 

# 3.5 -1.6

# ~ 3.8 2.8 3.-1 

# 2.3 3.-1

# ~ 3.3 2.1 

# 3.3 2.2 

# J6 E 3.9 3.0 

# _.:':..8

# .--~J-

.5-1
_ ---- ---- 

# 5.2 4.7 -1.7

# ~ -1.2 

# 3.4 -1.0 

# 3.0 

# l.J.. 2"5 

# 2.9 2.0 

# 2.2 1.6 

# JL J..2 

# 3.1 0.0 

# 3.-1 

# .QJl. 3.6 0.0 

# 3.6 0.0 -1.0 

# Jl.O 3.6 0.0 

# l.J.. .Q,Q. 3.-1 

# 0.0 

# 3.6 0.0 

# JJ.. 0.0 

# 3.7 0.0 

# 2.7 0.0 

# 2.6 

# ..c>Jl.. -1.7 

# 5.1 -1.0 

# 3.8 3.-1 

# 3.3 

# .3·1**~.O** 

# 2.6 .- 

## 1-- 

# 2.8 

# 2.2 2.6

• note some replacement values are affected by Stack A or 0 calibration data. These results are not used in subsequent Ibllhr calculations

# ArcelorMittal Mincora Mine Pellet Plant Replacement S02 Values Stacks Band C 

# TIME STAMP 

# STACK A STACK B STACKC STACK D Results Results Results Results 

# rep/aeemen rep/aeemen**~,** 

# S02Average S02Average 15 min interval ppm 

# Dry ppm 

# Dry Avg Avg 3/13/0813:00 2.2 2.4 2.6 3/13/08 13:15 4.4 3.4 3.1 2.8 3/13/08 13:30 4.5 3.4 3.1 2.7 3/13/08 13:45 3.2 2.7 2.6 2.5 3/13/0814:00 4.0 3.1 3/13/08 14:15 4.1 3/13/08 14:30 4.0 3/13/0814:45 2.7 3/13/0815:00 3/13/08 15:15 

# r=%.1==1 3/13/0815:30 3/13/08 15:45 3/13/08 16:00 3/13/0816:15 3/13/0816:30 3/13/0816:45 3/13/08 17:00 3/13/0817:15 3/13/0817:30 3/13/08 17:45 3/13/0818:00 3/13/08 18:15 3/13/08 18:30 3/13/08 18:45 3/13/08 19:00 3.8 3.3 3/13/0819:15 4.3 3/13/08 19:30 3/13/08 19:45 3/13/08 20:00 3/13/08 20:15 3/13/08 20:30 3/13/08 20:45 3/13/0821:00 3/13/0821:15 3/13/08 21:30 3/13/08 21:45 3/13/08 22:00 2.2 3/13/0822:15 3/13/08 22:30 3/13/08 22:45 3/13/08 23:00 3/13/08 23:15 3/13/08 23:30 3/13/08 23:45



# _ .. 

# 3/14/080:00**._._.~.** 

### ... 

## I.. 

# 3/14/08 0:15 . .. 

# 3/14/08 0:30 -"".



## -_. 

# 3/14/08 0:45 3/14/081:00 3/14/08 1:15 3/14/08 1:30 3/14/08 1:45 4.0 3/14/082:00 3/14/08 2:15 3/14/082:30 3/14/082:45 3/14/083:00 5.2 3/14/083:15 5.4 2.6 3/14/08 3:30 5.4 2.6 3/14/08 3:45 2.6 3/14/084:00 2.6 3/14/084:15 2.8 3/14/084:30 2.7 3/14/084:45 2.8 Barr Engineering Co. December 5, 2008

• note some replacement values are affected by Stack A or D calibration data. These results are not used in subsequent Ib/lhr calculations ArcelorMittal Mincora Mine Pellet Plant 

# TIME STAMP

15 min interval 

# 3/13/0813:00 3/13/08 13: 15 

# 3/13/08 13:30 3/13/08 13:45 3/13/0814:00 3/13/08 14:15 3/13/08 14:30 3/13/0814:45 3/13/0815:00 3/13/08 15: 15 

# 3/13/0815:30 3/13/08 15:45 3/13/08 16: 00 

# 3/13/0816:15 3/13/0816:30 3/13/0816:45 3/13/08 17:00 3/13/0817:15 3/13/0817:30 3/13/08 17:45 3/13/0818:00 3/13/08 18: 15 

# 3/13/08 18:30 3/13/08 18:45 3/13/08 19:00 3/13/0819:15 3/13/08 19:30 3/13/08 19:45 3/13/08 20:00 3/13/08 20: 15 

# 3/13/08 20: 30 

# 3/13/08 20:45 3/13/0821:00 3/13/0821:15 3/13/08 21 :30 

# 3/13/08 21:45 

# 3/13/08 22:00 3/13/0822:15 3/13/08 22:30 3/13/08 22:45 3/13/08 23:00 3/13/08 23: 15 

# 3/13/08 23:30 3/13/08 23:45 3/14/080:00 

# _ .. 

# 3/14/08 0: 15

.. 

# 3/14/08 0: 30 

# 3/14/08 0:45
_. 

# 3/14/081:00 3/14/08 1: 15 

# 3/14/08 1:30 

# 3/14/08 1:45 

# 3/14/082:00 3/14/08 2: 15 

# 3/14/082:30 3/14/082:45 3/14/083:00 3/14/083:15 3/14/08 3:30 3/14/08 3:45 3/14/084:00 3/14/084:15 3/14/084:30 3/14/084:45 Replacement S02 Values Stacks Band C 

# STACK A STACK B Results Results 

# rep/aeemen S02Average S02Average

ppm 

# Dry ppm 

# Dry

Avg Avg 2.3 2.2 4.4 3.4 4.5 3.4 3.2 2.7 4.0 3.1 4.1 3.3 4.0 3.1 2.7 2.3 2.6 2.2 

# STACKC STACK D Results Results 

# rep/aeemen SQ2Ave(age
. S02Average ··bomOi:\! 

# ppm 

# Dry .!
. 

# Avt;:l'<. Avg 

# 2..1 2.6 

# 3.1 2.8 

# 3.1 2.7 

# 2.6 2.5 

# 2.8 2.5 

# 2.9 2.6 

# 2.8 2.6 

# 2.3 2.3 

# 2.3 2.3 2.6 2.2 r=%.1==1=2.3 2.6 2.2 

# ·N

---- 3.5 2.8 3.2 2.6 2.-1 

# 2.3 3.5 2.8 

# 2.5 2.3 3.4 2.8 

# 2.5 2.2**~** 

# 4.5 3.5 

# 2.9 2.4

# I-~-# 

# H**~** 

# ._.. 

# 2.8

..

# -

# 1~ - 

# 2./ 3.8 3.0 

# 2.6 2.3 3.8 3.1 

# 2.6 2.2 3.6 3.1 

# 2.5 2.2 3.7 3.2 

# 2.5 2.2 3.4 3.1 

# 2.-1 2.1 3.7 3.3 

# 1.9 1.3 3.8 3.3 

# 2.6 2.2 4.3 3.6 

# 2./ 2.3 3.4 3.0 2.-1 

# 2.2 4.4 3.9 

# 2.8 2.3 5.6 4.7 

# 3.3 2.5 6.2 5.3 

# 3.5 2.6 4.9 4.2 3.0 

# 2.4 4.5 3.8 

# 2.8 2.3 3.8 3.3 

# 2.5 2.2 4.1 3.4 

# 2.6 2.2 3.5 3.2 2.-1 

# 2.1 3.4 3.0 2.-1 

# 2.1 3.1 2.8 

# 2.2 2.0 4.1 3.7 

# 2.6 2.2 6.0 5.1 

# 3.5 2.6 6.5 5.7 

# 3.8 2.8 6.0 5.1 

# 3.6 2.7 5.5 4.7 

# 3.2 2.4 5.0 4.4 3.0 ._- 

# 1.2 ._.- 

# 5.5 5.0 

# 3.3

.. ... 

# 7.0
....

# ---t.~. 

# - I·

# -~+ 6.8
.. _ .....

....

## - .. 

## - 

# 6.5 5.9 

# 3./

.. 

# 5.0 4.4 3.U 

# _ .. 

# 4.0 3.7 

# 2.5 2.1 4.1 3.7 

# 2.6 2.2 4.4 4.1 

# 2.8 2.3 4.4 4.0 

# 2./ 2.2 3.0 3.0 

# 2.2 2.0 4.3 3.9 

# 2./ 2.2 4.5 4.0 

# 2.8 2.3 5.3 4.7 

# 3.2 2.4 5.2 4.7 

# 3.1 2.5 5.4 4.9 

# 3.3 2.6 5.4 4.9 

# 3.3 2.6 5.6 5.0 

# 3.3 2.6 5.6 5.1 

# 3.3 2.6 6.2 5.6 

# 3./ 2.8 5.5 5.0 3.-1 

# 2.7 6.0 5.4 

# 3.6 2.8 Barr Engineering Co. December 5, 2008

• note some replacement values are affected by Stack A or D calibration data. These results are not used in subsequent 

# Ib/lhr calculations

# ArcelorMittal Mincora Mine Pellet Plant Replacement S02 Values Stacks Band C 

# TIME STAMP 

# STACK A STACK B STACK C STACK D Results Results Results Results 

# replacemen replacemen S02Average S02 Average S02 Average 15 min interval POI I 

# Dry ppm Dry ppm Dry 

# /l ;j 

# Avg 

# 3/14/08 5:00 3/14/085:15 3/14/08 5:30 3/14/08 5:45 3/14/086:00 6.1 

# 3/14/08 6:15 6.4 

# 3/14/08 6:30 6.8 

# 4.4 3.8 

# 3/14/086:45 7.3 6.4 

# 4.7 4.0 

# 3/14/087:00 6.8 

# 4.3 3.5 

# 3/14/087:15 5.6 

# 3.6 3.0 

# 3/14/087:30 6.0 2.9 

# 3/14/087:45 5.8 3.0 

# 3/14/088:00 4.7 

# 3/14/088:15 2.8 

# 3/14/08 8:30 3/14/088:45 3/14/089:00

_. 

# 3/14/08 9:15 

# 3/14/089:30 3/14/089:45 3/14/08 10:00

- 

## -I. 

# 3/14/0810:15 -I..

...... 

# -_. 

# 3/14/08 10:30

.. 

# 3/14/08 10:45 

# 3/14/08 11:00 

# 3/14/0811:15 I.t 

# 3/14/08 11:30 

# 3/14/08 11:45

.. 

# 3/14/0818:00 3.7 2.6 

# 3/14/0818:15 3/14/0818:30 .0 

# 3/14/08 18:45 3/14/08 19:00 3/14/0819:15 3/14/08 19:30 3/14/0819:45 3/14/0820:00 3/17/0814:00 4.7 3.8 

# 3/17/0814:15 4.9 

# 3/17/0814:30 5.3 

# 3/17/0814:45 5.2 

# 3/17/08 15:00 4.8 

# 3/17/08 15:15 4.9 

# 3/17/0815:30 3/17/0815:45 3/17/0816:00 3/17/0816:15 3/17/0816:30 3/17/08 16:45 3/17/0817:00 3/17/0817:15 3/17/0817:30 3/17/0817:45 ._ ... 

# 3/17/0818:00 3/17/0818:15 3/17/0818:30 3/17/0818:45 3/17/0819:00 3/17/0819:15 3/17/0819:30 3/17/08 19:45 3/17/08 20:00 Barr Engineering Co. December 5, 2008

• note some replacement values are affected by Stack A or D celibration data. These results are not used in subsequent Ibllhr calculations 

# ArcelorMittal Mincora Mine Pellet Plant

_. 

# TIME STAMP

15 min interval 

# 3/14/08 5:00 3/14/085:15 3/14/08 5:30 3/14/08 5:45 3/14/086:00 3/14/08 6: 15 

# 3/14/08 6: 30 

# 3/14/086:45 3/14/087:00 3/14/087:15 3/14/087:30 3/14/087:45 3/14/088:00 3/14/088:15 3/14/08 8:30 3/14/088:45 3/14/089:00 3/14/08 9: 15 

# 3/14/089:30 3/14/089:45 3/14/08 10:00 

# 3/14/0810:15 3114/08 10: 30 

# 3/14/08 10:45 

# 3/14/08 11 :00 

# 3/14/0811:15 3/14/08 11 :30 

# 3/14/08 11:45 

# 3/14/0818:00 3/14/0818:15 3/14/0818:30 3/14/08 18:45 3/14/08 19:00 3/14/0819:15 3/14/08 19:30 3/14/0819:45 3/14/0820:00 3/17/0814:00 3/17/0814:15 3/17/0814:30 3/17/0814:45 3/17/08 15:00 3/17/08 15:15 3/17/0815:30 3/17/0815:45 3/17/0816:00 3/17/0816:15 3/17/0816:30 3/17/08 16:45 3/17/0817:00 3/17/0817:15 3/17/0817:30 3/17/0817:45 3/17/0818:00 3/17/0818:15 3/17/0818:30 3/17/0818:45 3/17/0819:00 3/17/0819:15 3/17/0819:30 3/17/08 19:45 3/17/08 20:00 Replacement S02 Values Stacks Band C 

# STACK A STACK B Results Results 

# replacemen S02Average S02 Average

ppm Dry ppm Dry

Avg Avg 5.3 4.8 5.1 4.7 6.1 5.4 6.1 5.5 6.1 5.5 6.4 5.8 6.8 6.0 7.3 6.4 6.8 5.9 5.6 5.5 6.0 5.3 5.8 5.2 6.3 5.6 6.3 5.5 6.1 5.3 6.5 5.6 6.6 5.6 6.7 5.8 7.3 6.2 7.0 6.0 7.2 6.4

- 

# _. 6.8 6.5 6.8 6.3

- 

# 6.3 5.8 6.4 5.8 6.5 5.8 6.3 5.5 6.8 6.1 6.9 5.2 8.2 6.2 7.1 5.4 6.1 4.7 6.6 5.1 6.5 5.0 6.5 4.9 6.4 4.9 6.2 4.8 4.7 3.8 4.9 3.9 5.3 4.1 5.2 4.0 4.8 3.8 4.9 3.7 4.8 3.7 4.8 3.7 5.2 4.1 4.7 3.6 3.8 3.0 3.4 2.8 4.0 3.1 4.2 3.4 5.2 4.0 

# STACK C Results 

# replacemen**S02Av~rage** 

# ppm Dry

Avq··· 

# .. 3.2 3.1 3.6 3.7 3.7 -1.1 -1.-1 -1.7 -1.3 3.6 3.7 3.6 -1.9 3.7 3.6 3.9 -1.1 3.1 -1.2 3.8 -1.1 -1.-1 -1.5 

# 3.9 -1.0 

# 3.9 3.8 -1.3 3.7 -1.-1 

# 3.8 3.3 3.6 3.6 3.5 3.5 3.5 3.-1 3.3 3.3 3.1 3.0 2.9 2.8 2.7 2.9 2.6 2.2 2.1 2.3 2.5 2.9

.... .. 

# 5.1 

# .-

# ---~:~ ...... 

# jJ

..... 

# 5.5 5.6 4.5 

# 3.1 4.7 3.7 

# 2.7 4.8 3.9 

# 2.7 4.4 3.8 

# 2.7 5.4 4.4 

# 3.0 5.6 4.6 

# 3.1 5.9 4.8 

# 3.2 5.0 4.1 

# 2.8 Barr Engineering Co. December 5, 2008 

# STACK D Results S02 Average

ppm Dry

Avg 2.6 2.5 2.7 2.9 2.9 3.4 3.8 4.0 3.5 3.0 2.9 3.0 4.7 2.8 2.8 3.0 3.3 1.8 3.2

-----**~I** 

# ____

.. .. 

# _- 

# '3.2-
....

3.2 31 3.1 3.5

.. 

# 2.6 3.0 2.6 2.3 2.5 2.6 2.5 2.5 2.6 3.1 2.9 2.7 2.5 2.4 2.3 2.2 2.0 2.1 1.8 1.7 1.7 1.8 1.9

# ~1 .... 

# 2-:1

- 

# .¥O

._. 

# 2.0 2.1 2.3 2.3 2.2 2.0

• note some replacement values are affected by Stack A or D celibration data. These results are not used in subsequent Ib/lhr calculations

# ArcelorMittal Mincora Mine Pellet Plant Replacement S02 Values Stacks Band C 

# TIME STAMP 

# STACK A STACK B STACKC STACKD Results Results Results Results replacemen replacemen S02Average S02Average S02 Average 15 min interval 

# POIhDr\! ppm Dry ppm Dry 

# I- Avg Avg 3/17/0820:15 3.0 2.2 

# 1.8 3/17/0820:30 3.7 2.6 

# 1.9 3/17/08 20:45 4.3 2.6 

# 1.4 3/18/0810:00 3. 

# 3/18/0810:15 -I.. 

# 3/18/08 10:30 -I. 

# 3/18/08 10:45 -I.. 

# 3/18/0811:00 -I. 

# 3/18/0811:15 -I. 

# 3/18/08 11:30 -I. 

# 3/18/08 11:45 3.. 

# 3/18/08 12:00 3/18/0812:15 3/18/0812:30 3/18/08 12:45 3/18/0813:00 3/18/08 13:15 5.1 0 3/18/08 13:30 6.3 5.3 

# 9 3.2 3/18/0813:45 6.6 3.7 3/18/0814:00 6.7 3/18/0814:15 6.5 3/18/0814:30 6.3 3/18/0814:45 3/18/08 15:00 3/18/0815:15 3/18/08 15:30 3/18/08 15:45 3/18/0816:00 3/18/08 16:15 3/18/08 16:30 3/18/08 16:45 -1.-1 

# 3/18/0817:00 3/18/0817:15 3/18/0817:30 3/18/08 17:45 3/18/0818:00 3/18/0818:15 3/18/08 18:30 3/18/08 18:45 3/18/0819:00 8.2 3/18/0819:15 3/18/08 19:30 3/18/08 19:45 3/18/08 20:00 3/18/08 20:15 3/18/08 20:30 3/18/08 20:45 3/18/0821:00 3/18/0821:15 3/18/08 21:30 3/18/08 21:45 3/18/08 22:00 3/18/08 22:15 3/18/08 22:30 5.6 2.5 3/18/08 22:45 5.6 3/18/08 23:00 5.3 3/18/0823:15 3/18/08 23:30 3/18/08 23:45 3/19/08 0:00 3/19/08 0:15 ._- 

# 3/19/08 0:30 3/19/08 0:45 

# ._ ..... 

# Barr Engineering Co. December 5. 2008

* 

# note some replacement values are affected by Stack A or D calibration data. These results are not used in subsequent Ibllhr calculations ArcelorMittal Mincora Mine Pellet Plant 

# TIME STAMP

15 min interval 

# 3/17/0820:15 3/17/0820:30 3/17/08 20:45 3/18/08 10:00 

# 3/18/0810:15 3/18/08 10: 30 

# 3/18/08 10:45 

# 3/18/0811:00 3/18/0811:15 3/18/08 11 :30 

# 3/18/08 11:45 

# 3/18/08 12:00 3/18/0812:15 3/18/0812:30 3/18/08 12:45 3/18/0813:00 3/18/08 13: 15 

# 3/18/08 13:30 3/18/0813:45 3/18/0814:00 3/18/0814:15 3/18/0814:30 3/18/0814:45 3/18/08 15:00 3/18/0815:15 3/18108 15:30 3/18/08 15:45 3/18/0816:00 3/18/08 16: 15 

# 3/18/08 16:30 3/18108 16:45 311810817:00 

# 3118/0817:15 3/18/0817:30 3/18/08 17:45 3/18/0818:00 3/18/0818:15 3/18/08 18:30 3/18108 18: 45 

# 3118/0819:00 3/18/0819:15 3/18/08 19:30 3/18/08 19:45 3/18/08 20:00 3/18/08 20: 15 

# 3/18108 20:30 3/18/08 20:45 3/18/0821:00 3/18/0821:15 3/18/08 21 :30 

# 3/18/08 21:45 

# 3/18/08 22:00 3/18/08 22: 15 

# 3/18/08 22: 30 

# 3/18/08 22:45 3/18/08 23:00 3/18/0823:15 3/18/08 23:30 3/18/08 23:45 3119/08 0:00 3/19/08 0: 15 

# 3/19/08 0:30 3/19/08 0:45 Replacement S02 Values Stacks Band C 

# STACK A STACK B Results Results replacemen S02Average S02Average

ppm 

# Dry ppm Dry

Avg Avg 3.5 3.0 4.4 3.7 5.5 4.3 4.0 4.9 7.1 5.5 7.0 5.3 6.7 5,0 6.7 5.1 6.8 5.2 6.9 5.2 6.2 4.7 6.7 5.1 6.7 5.2 6.3 4.9 6.1 4.6 5.9 4.5 6.4 5.1 6.3 5.3 6.6 5.7 6.7 5.8 6.5 5.6 6.3 5.4 6.2 5.2 6.1 5.2 6.3 5.3 6.8 5.8 6.7 5.8 7.0 5.9 7.0 5.9 7.5 6.4 6.9 5.8 7.1 6.0 7.8 6.6 7.9 6.8 8.3 7.2 8.0 3.0 8.0 7.0 7.8 6.9 8.4 7.2 8.2 7.1 7.8 6.7 8.2 7.1 7.7 6.6 8,0 6.9 7.7 6.8 7.4 6.5 7.8 6.7 7.1 6.1 6.9 5.9 7.2 6.0 6.2 5.1 6.1 4.9 5.8 4.6 5.6 4.5 5.6 4.5 5.3 4.3 5.0 4.1 5.0 4.3 4.9 4.4 5.7 4.6 5.2 4.1 4.3 3.4 3.4 2.5 Barr Engineering Co. December 5, 2008 

# STACKC STACKD Results Results replacemen S02Average S02 Average 

# i··PPlTlDry ppm Dry

". 

# >Avg Avg 2.2 1.8 2.6 1.9 2.6 1.4 1·2 3.2

. 

# _ ... 

# -1.-1 3.6 -1.3 3.5 -1.2 3.4 -1.1 3.3 -1.3 3.5 -1.2 3.3 .- 

# 3.8 3.1 -1.2 3.4 .- 

# -1.2 3.4 -1.2 3.6 3.9 3.3 3.7 3.0 -1.0 

# 3.3 3.9 3.2 -1.-1 3.7 -1.5 4.0 -1.-1 3.9 -1.3 3,7 -1.1 3.5 -1.0 

# 3.4 -1.1 3.5 -1.5 3.9 -1.6 4.0 -1.6 3.9 -1.5 3.7 5.0 

# 4.4 -1.-1 3.7 -1.7 4.0 5.2 4.5 5.-1 4.7 6.0 

# 5.5 

# Jil 6.1 5.0 

# 4.1 6.0 

# 5.7 6.3 6.0 6.2 5.8 5.8 5.3 6.3 6.0 5.7 5.3 6.1 5.8 6.-1 6.4 5.8 5.6 5.9 5.5 5.1 4.6 -1.8 4.3 -1.6 3.8 3.6 2.7 3.-1 2.5 3.3 2.4 3.3 2.5 3.3 2,6 3.1 2.3 2.9 2.2 3.1 2.5 3.-1 3.0 3.6 3.0 3.2 2.5**~** 

## --- 

# 2.-1

# +~-'= 1.8

* note some replacement values are affected by Stack A or D calibration data. These results are not used in subsequent Ibllhr calculations

# ArcelorMittal Mincora Mine Pellet Plant Replacement S02 Values Stacks Band C 

# TIME STAMP 

# STACK A STACK B STACKC STACK D Results Results Results Results 

# replacemen replacemen ;S02j\veraget S02 Average S02Average 15 min interval 

# mD ppm Dry ppm Dry Avg Avg 

# 3/19/08 1:00 2.4 

# 1.7 1.1 

# 3/19/081:15 2.8 

# 1.9 1.3 

# 3/19/08 1:30 

# 3/19/08 1:45 

# 3/19/08 2:00 3.5 

# 3/19/08 2:15 

# 3/19/08 2:30 3/19/08 2:45 3/19/08 3:00 3/19/083:15 3/19/08 3:30 3/19/08 3:45 3/19/08 4:00 3/19/084:15 3/19/084:30 ,--- 

# 3/19/08 4:45 3/19/08 5:00 

# . ./



# - 3/19/085:15 

# .8 3/19/08 5:30 

# .8 3/19/08 5:45 

# .7 3/19/086:00 3/19/086: 15 3/19/08 6:30 3/19/08 6:45 3/19/08 7:00 3/19/08 7:15 5.7 

# 3/19/087:30 5.4 

# 3/19/08 7:45 4.5 

# 3/19/08 8:00 3/19/088:15 3/19/08 8:30 3/19/08 8:45 3/19/089:00 3/19/089:15 3/19/08 9:30 3/19/08 9:45 3/19/08 10:00 

# 3/19/0810:15 3/19/08 10:30 

# 3/19/08 10:45 

# 3/19/08 11 

# :00 

# 3/19/0811:15 3/19/0811:30 3/19/08 11:45 

# 3/19/08 12:00 3/19/08 12:15 

# 3/19/08 12:30 3/19/08 12:45 3/19/0813:00 3/19/0813:15 3/19/08 13:30 3/19/08 13:45 3/19/08 14:00 3/19/0814:15 3/19/08 14:30 3/19/0814:45 4.9 

# 3/19/0815:00 4.7 

# 3/19/0815:15 2.6 

# 3/19/08 15:30 2.3 

# 3/19/0815:45 2.4 

# 3/19/08 16:00 2.5 

# 3/19/08 16:15 2.6 

# 3/19/0816:30 2.7 

# 3/19/0816:45 

# 3.5 2.7 Barr Engineering Co. December 5, 2008

• note some replacement values are affected by Stack A or D calibration data. These results are not used in subsequent Ibllhr calculations ArcelorMittal Mincora Mine Pellet Plant 

# TIME STAMP

15 min interval 

# 3/19/08 1:00 

# 3/19/081:15 3/19/08 1:30 

# 3/19/08 1:45 

# 3/19/08 2:00 3/19/08 2: 15 

# 3/19/08 2:30 3/19/08 2:45 3/19/08 3:00 3/19/083:15 3/19/08 3:30 3/19/08 3:45 3/19/08 4:00 3/19/084:15 3/19/084:30 3/19/08 4:45 3/19/08 5:00 3/19/085:15 3/19/08 5:30 3/19/08 5:45 3/19/086:00 3/19/086: 15 3/19/08 6:30 3/19/08 6:45 3/19/08 7:00 3/19/08 7: 15 

# 3/19/087:30 3/19/08 7:45 3/19/08 8:00 3/19/088:15 3/19/08 8:30 3/19/08 8:45 3/19/089:00 3/19/089:15 3/19/08 9:30 3/19/08 9:45 3/19/08 10:00 

# 3/19/0810:15 3/19/08 10:30 

# 3/19/08 10:45 

# 3/19/08 11 :00 

# 3/19/0811:15 3/19/0811:30 3/19/08 11:45 

# 3/19/08 12:00 3/19/08 12: 15 

# 3119/08 12:30 3119/08 12:45 3/19/0813:00 3/19/0813:15 3/19/08 13:30 3/19/08 13:45 3/19/08 14:00 3/19/0814:15 3/19/08 14:30 3/19/0814:45 3/19/0815:00 3/19/0815:15 3/19/08 15:30 3/19/0815:45 3/19/08 16:00 3/19/08 16: 15 

# 3/19/0816:30 3/19/0816:45 Replacement S02 Values Stacks Band C 

# STACK A STACK B Results Results 

# replacemen S02Average S02Average

ppm 

# Dry ppm 

# Dry

Avg Avg 3.2 2.4 3.7 2.8 2.8 2.1 3.0 2.4 3.5 2.1 3.3 1.7 3.1 1.7 2.6 1.4 3.3 1.8 2.8 1.5 3.8 2.0 2.9 1.5 3.4 1.7 36 1.7 2.8 

# -h}**~---** 2.5

- 

# 2.8 1.1 3.6 1.1 3.5 1.1 3.4 1.1 3.4 1.0 3.3 0.9 2.7 0.7 3.4 1.6 4.1 2.8 5.7 3.0 5.4 4.1 4.5 3.3 4.8 3.6 5.1 3.7 5.3 3.9 5.6 4.2 5.1 3.9 5.2 3.8 4.4 3.3 4.7 3.5 5.0 3.7 5.7 4.2 5.7 4.4 5.5 4.5 5.1 4.1 5.0 4.1 4.9 3.8 4.7 3.8 5.3 4.2 5.3 4.3 5.2 4.2 4.9 3.9 5.0 4.1 5.3 4.3 5.4 4.4 5.9 4.8 5.5 4.5 5.4 4.5 5.8 4.7 6.2 4.9 5.9 4.7 5.8 4.5 5.1 4.0 5.5 4.3 5.4 4.2 5.8 4.5 5.5 4.4 6.1 4.7 Barr Engineering Co. December 5, 2008 

# STACKC STACK D Results Results 

# replacemen S02Average S02Average 

# ,'ppm 

# 01)1 ppm 

# Dry



# ...... Avg Avg 1.7 1.1 1.9 1.3 1.5 1.0 1.6 1.1 1.8 1.1 1.6 1.0 1.5 0.9 1..1 0.9 1.6 1.0 1.-1 0.9 1.9 1.2 1.5 0.9 1.7 1.0-- 1.9 

# E ._.- 

# 1.-1 

# L?.. .... 

# O.B**.--~**



## ---- -- 

# - 1.8 1.2 1.8 1.2 1.7 

# 1.0 1.6

--

# i--*

..

## - 

# 1.5 

# 1.3 0.7 1.5 

# 0.8 2.0 

# 1.2 2.7 1.6 2.8 1.9 2.5 1.8 -1.0 

# 4.0 2,9 2.1 2.9 2.1 3.1 2.3 2.9 2.2 2.6 1.6 2.6 2.0 2.7 2.1 2.9 2.2 3.3 2.5 3.-1 2.6 3.3 2.6 3.1 2.5 3.1 

# 2.5 2.9 2.3 2.9 2.3 3.1 

# 2.4 3.1 

# 2.4 3.1 

# 2.4 2.9 2.3 3.0 

# 2.4 3.2 2.5 3.3 2.7 3.6 2.9 3.3 2.6 3.3 2.6 3.5 2.7 3.7 2.9 3.5 2.8 3.-1 2.6 3.0 

# 2.3 3.2 2.4 3.3 2.5 3.-1 2.6 3.-1 2.7 3.5 2.7

• note some replacement values are affected by Stack A or D calibration data. These results are not used in subsequent Ibllhr calculations

# ArcelorMittal Mincora Mine Pellet Plant Replacement S02 Values Stacks Band C 

# TIME STAMP STACK A STACK B STACK C STACK D Results Results Results Results 

# replacemen replacemen S02Merage S02Ave S02 Average 15 min interval pp nDrv ppm Dry ppm Dry Avg Avg 

# 3/19/08 17:00 4.5 

# 3/19/0817:15 5.0 

# 3/19/08 17:30 4.5 

# 3/19/0817:45 4.2 

# 3/19/08 18:00 4.2 

# 3/19/08 18:15 5.8 4.5 

# 3.5 3/19/08 18:30 5.7 4.6 

# 3.6 2.9 

# 3/19/08 18:45 6.7 5.6 

# 4.4 3.7 

# 3/19/08 19:00 7.5 6.1 

# 5.1 4.5 

# 3/19/0819:15 7.1 5.8 

# 4.7 

# 3/19/0819:30 6.3 

# 3/19/08 19:45 6.0 

# 3/19/08 20:00 6.1 

# 3/19/08 20:15 

# 3/19/08 20:30 3/19/08 20:45 3/19/0821:00 3/19/0821:15 3/19/08 21:30 

# 3/19/08 21:45 

# 3/19/08 22:00 3/19/08 22:15 

# 3/19/08 22:30 

# , .c 3/19/08 22:45 3/19/08 23:00 3/19/0823:15 3/19/08 23:30 

# 3/19/08 23:45 3/20108 0:00 3/20108 0:15 

# 3/20108 0:30 3/20108 0:45 3/20108 1:00 

# 3/20108 1:15 

# 3/20108 1:30 

# 3/20108 1:45 

# 3/20108 2:00 3/20108 2:15 

# 3/20108 2:30 3/20108 2:45 3/20108 3:00 3/20108 3:15 

# 3/201083:30 3.5 

# 3/20108 3:45 3.8 

# 3/20108 4:00 3/201084:15 3/20108 4:30 3/20108 4:45 3/201085:00 3/201085:15 3/20108 5:30 3/20108 5:45 3/20108 6:00 .- 

# 3/201086:15 3/20108 6:30 3/20108 6:45 3/20108 7:00

. 

# 3/20108 7:15 

# 3/201087:30 3/20108 7:45 3/20108 8:00 3/201088:15 3/20108 8:30 3/20108 8:45 Barr Engineering Co. December 5, 2008

* 

# note some replacement values are affected by Stack A or D calibration data. These results are not used in subsequent Ibllhr calculations ArcelorMittal Mincora Mine Pellet Plant 

# TIME STAMP

15 min interval 

# 3/19/08 17:00 3/19/0817:15 3/19/08 17:30 3/19/0817:45 3119/08 18:00 3/19/08 18: 15 

# 3/19/08 18:30 3/19/08 18:45 3/19/08 19:00 3/19/0819:15 3/19/0819:30 3/19/08 19:45 3/19/08 20:00 3/19/08 20: 15 

# 3/19/08 20:30 3/19/08 20:45 3/19/0821:00 3/19/0821:15 3/19/08 21 :30 

# 3/19/08 21 :45 

# 3/19/08 22:00 3/19/08 22: 15 

# 3/19/08 22: 30 

# 3/19/08 22:45 3119/08 23:00 3/19/0823:15 3/19/08 23: 30 

# 3/19/08 23:45 3/20108 0:00 3/20108 0: 15 

# 3/20108 0:30 3/20108 0:45 3/20108 1:00 

# 3/20108 1: 15 

# 3/20108 1:30 

# 3/20108 1:45 

# 3/20108 2:00 3/20108 2: 15 

# 3/20108 2:30 3/20108 2:45 3/20108 3:00 3/20108 3: 15 

# 3/201083:30 3/20108 3:45 3/20108 4:00 3/201084:15 3/20108 4:30 3/20108 4:45 3/201085:00 3/201085:15 3/20108 5:30 3/20108 5:45 3/20108 6:00 3/201086:15 3/20108 6:30 3/20108 6:45 3/20108 7:00 3/20108 7: 15 

# 3/201087:30 3/20108 7:45 3/20108 8:00 3/201088:15 3/20108 8:30 3/20108 8:45 Replacement S02 Values Stacks Band C 

# STACK A STACK B Results Results 

# replacemen S02Average S02Average

ppm Dry ppm Dry

Avg Avg 5.8 4.5 6.4 5.0 5.8 4.5 5.2 4.2 5.5 4.2 5.8 4.5 5.7 4.6 6.7 5.6 7.5 6.1 7.1 5.8 6.3 5.1 6.0 4.9 6.1 4.9 6.0 4.8 6.1 4.9 5.9 4.9 5.9 4.8 5.8 4.7 5.2 4.2 4.8 3.8 4.8 3.8 4.9 3.8 4.4 3.6 5.3 4.2 5.0 3.9 5.1 4.1 5.0 3.9 4.5 3.6 4.8 3.9 4.9 4.0 4.4 3.5 4.2 3.3 3.9 3.0 3.9 2.9 4.9 3.7 4.1 3.1 3.9 3.0 4.2 3.6 4.3 3.1 3.6 2.5 4.1 2.9 4.5 3.2 4.7 3.5 5.1 3.8 5.2 4.0 5.6 4.3 6.1 5.1 6.3 5.2 5.7 4.8 5.9 4.9 6.4 5.2 5.4 4.3 5.4 4.2 5.9 4.6 5.3 4.3 5.0 3,9 4.9 3.8 4.6 3.6 5.3 5.0 5.6 4.4 5.4 4.4 6.0 4.8 5.9 5.1 6.6 5.6 Barr Engineering Co. December 5, 2008 

# STACK C STACK D Results Results 

# replacemen S02AVerage S02 Average ····.···.PPmDry· ppm Dry

... 

# Avg Avg 

# 3.5 2.7 

# 3.8 3.0 

# 3.5 2.7 

# 3.1 2.4 

# 3.2 2.4 

# 3.5 2.7 

# 3.6 2.9 -1.-1 

# 3.7 

# 5.1 4.5 -1.7 

# 4.0 -1.2 

# 3.6 -1.0 

# 3.5 

# 3.9 3.2 

# 3.7 3.0 

# 3.8 3.0 

# 3.9 3.3 

# 3.9 33 

# 3.8 3.2 

# 3.3 2.8



# -- 3JI 

# 2.5 3.0 

# 2.5 

# 3.1 

# 1J-- 3.0

-- 

# 3.-1 

# ¥S

-- 3.1

---- 

# 1-- 3.3 2.7
__ 

# 3.2 2.6 

# 2.3 1.4 3.0 

# 2.5 ._--- 

# 3.0 

# 2.4 

# 2.8 2.3 

# 2.6 2.2 

# 2.5 2.1 

# 2.5 2.1 

# 2.9 2.3 

# 2.6 2.1 

# 2.1 1.5 

# 2.-1 1.8 

# 2.2 1.4 

# 1.9 1.3 2.-1 

# 1.8 

# 2.7 2.1 

# 2.8 2.2 3.0 

# 2.3 

# 3.2 2.5 3.-1 

# 2.7 -1.0 

# 3.4 

# -1.-1 4.0 

# 3.9 3.4 

# 3.9 3.4 

# -1.1 3.4

-- 

# 3.2 2.5 

# 3.3 

# 2§..

-- 

# 3.5

-- 

# 3.2 

# 2.5 2.9 

# ---g--- 2.9 2.8 

# 2.2 3.2 2.5 

# 3.-1 2.6 

# -1.3 4.2 

# 3.7 3.0 

# 3.6 2.8 

# 3.8 2.9

* 

# note some replacement values are affected by Stack A or D calibration data. These results are not used in subsequent Ib/lhr calculations

# ArcelorMittal Mincora Mine Pellet Plant Replacement S02 Values Stacks Band C 

# TIMESTAMP 

# STACK A STACK B STACKC STACK D Results Results Results Results 

# repJacemen repJacemen**c::n~l>',6r<,n'"** 

# S02Average S02 Average 15 min interval 

# DPll'lDfY ppm 

# Dry ppm 

# Dry 

# Ava Avg Avg 3/20/08 9:00 6.8 

# 4.0 3/20/08 9:15 7.4 4. 

# 3/20/08 9:30 4.. 

# 3/20/08 9:45 4. 

# 3/20/08 10:00 --_. 

# 3/20/08 10:15 3/20/08 10:30 - -- 

# _ .. 

## - 

# 3/20/08 10:45 3/20/08 11:00 3/20/0811:15 3/20/08 11:30 3/20/08 11:45 3/20/08 12:00 3/20/08 12:15 

# '.' 3/20/08 12:30 3/20/08 12:45 

# .c 3/20/08 13:00 3/20/08 13:15 3/20/08 13:30 3/20/08 13:45 3/20/08 14:00 2.8 5.. 

# 3/20/0814:15 7. 

# 3/20/08 14:30 7.9 

# 3/20/08 14:45 3/20/08 15:00 3/20/0815:15 3/20/08 15:30 3/20/08 15:45 3/20/08 16:00 3/20/0816:15 3/20/08 16:30 3/20/08 16:45 3/20/08 17:00 3/20/08 17:15 3/20/08 17:30 3/20/08 17:45 3/20/08 18:00 3/20/0818:15 3/20/0818:30 3/20/08 18:45 3/20/08 19:00 3/20/08 19:15 3/20/08 19:30 3/20/08 19:45 6.0 3/20/08 20:00 3/20/08 20:15 3/20/08 20:30 3/20/08 20:45 3/20/08 21:00 6.7 3.5 3/20/0821:15 4.4 3/20/08 21:30 4.6 3/20/08 21:45 4.9 3/20/08 22:00 4.6 3/20/08 22:15 4.5 3/20/0822:30 3/20/08 22:45 3/20/08 23:00 

# .c 3/20/0823:15 3/20/08 23:30 3/20/08 23:45 2.0 3/21/080:00 2.3 3/21/080:15 2.2 3/21/080:30 

# 4A 2.5 3/21/080:45 

# 4A 2.4 Barr Engineering Co. December 5, 2008

• note some replacement values are affected by Stack A or D calibration data. These results are not used in SUbsequent Ib//hr calculations ArcelorMitlal Mincora Mine Pellet Plant 

# TIMESTAMP

15 min interval 

# 3/20108 9:00 3/20108 9: 15 

# 3/20108 9:30 3/20108 9:45 3/20108 10:00 

# 3/20108 10: 15 

# 3/20108 10:30 

# 3/20108 10:45 

# 3/20108 11 :00 

# 3/2010811:15 3/20108 11 :30 

# 3/20108 11:45 

# 3/20108 12: 00 

# 3/20108 12: 15 

# 3/20108 12:30 3/20108 12:45 3/20108 13:00 3/20108 13: 15 

# 3/20108 13:30 3/20108 13:45 3/20108 14:00 3/2010814:15 3/20108 14:30 3/20108 14:45 3/20108 15:00 3/2010815:15 3/20108 15:30 3/20108 15:45 3/20108 16:00 3/2010816:15 3/20108 16:30 3/20108 16:45 3/20108 17:00 3/20108 17:15 3/20108 17:30 3/20108 17:45 3/20108 18:00 3/2010818:15 3/2010818:30 3/20108 18:45 3/20108 19:00 3/20108 19: 15 

# 3/20108 19:30 3/20108 19:45 3/20108 20:00 3/20108 20: 15 

# 3/20108 20: 30 

# 3/20108 20:45 3/20108 21 :00 

# 3/2010821:15 3/20108 21 :30 

# 3/20108 21:45 

# 3/20108 22:00 3/20108 22: 15 

# 3/2010822:30 3/20108 22:45 3/20108 23:00 3/2010823:15 3/20108 23:30 3/20108 23:45 3/21/080:00 3/21/080:15 3/21/080:30 3/21/080:45 Replacement S02 Values Stacks Band C 

# STACK A STACK B Results Results replacemen S02Average S02Average

ppm Dry ppm Dry

AVQ Avg 6.8 5.6 7.4 5.8 7.1 5.6 7.3 5.7 7.7 6.1 8.3 

# STACKC Results replacemen SQ2Average 1<.ppmDry. 

# Ai/g .... -1.0 ./..1 

# -1.2 -1.-1 -1.8 5.0 

# it

--- - 

# 7.0 

# n 6.4 5.0 

# 3.7 7.2 5.8 -1.2 

# 8.1 6.4 -1.9 

# 8.9 7.3 6.0 

# 8.3 6.9 

# 5.5 8.4 6.9 

# 5.5 8.8 7.4 

# 5.8 8.6 7.2 

# 5.6 8.7 

# 7.6 5.7 8.5 

# 7.1 4.8 8.7 7.-1 

# 5.1 8.3 7.-1 

# 5.1 8.7 

# 7.3 6.0 2.8 

# 5.8 1.9 8.1 

# 7.8 5.2 8.6 

# 7.9 5.4 8.0 

# 6.9 4.7 7.8 

# 6.6 4.5 8.2 

# 7.3 4.9 9.4 

# 8.8 6,0 8.4 

# 7.8 5.3 8.4 

# 8.1 5.5 8.4 

# 7.7 5.2 8.6 8.0 

# 5.4 8.2 

# 7.9 5.4 7.3 7.0 

# 4.7 7.2 

# 6.6 4.5 6.8 6.0 

# 1.4

.. 

## - 

# 6.6 

# 6.2 4.2 6.4 

# 5.9 4.0 6.4 

# 5.8 3.9 6.7 

# 6.3 2.6 6.2 6.0 

# 3.9 6.9 

# 6.3 4.2 6.5 

# 5.6 3.8 5.9 -1.8 

# 1.9 6.0 -1.8 

# 3.7 6.0 -1.9 

# 3.9 5.9 5.0 

# 3.9 5.9 -1.9 

# 3.9 6.0 

# 5,1 4.1 6.7 

# 5.7 4.5 6.1 

# 5.2 4.4 7.0 

# 5.8 4.6 7.2 

# 5.9 4.9 6.8 

# 5.8 4.6 6.6 

# 5.7 4.5 6.6 

# 5.8 4.5 5.4 -1.2 

# 3.4 5.4 -1.0 

# 3.1 4.5 3.-1 

# 2.7 4.2 

# 3.2 2.4 4.8 

# 3.6 2.8 5.9 -1.-1 

# 3.5 5.1 

# 3.9 3.1 5_7 -1.-1 

# 3.6 5.8 -1.-1 

# 3,6 Barr Engineering Co. December 5, 2008 

# STACK D Results S02 Average

ppm Dry

Avg 3.1 3.5 3.3
___ . __

# ~----

--- 

# _.- 3.2 2.8 3.1 -_. 

# 3.8 5.2 4.8 4.6 4.9 4.8 4.8 4.3 4.5 4.7 4.4 5.5 5.4 5.2 4.3 4.0 4.6 5.9 5.2 5.5 5.0 5.2 5.4 4.7 4.4 3.8

-- 

# 4.2 3.8 3.8 4.2

_ 

### .. 

## - 

# 4.1 4.1 3.5 2.9 2.8 2.9 3.0 2.9 3.2 3.5 3.2 3.5 3.5 3.5 3.6 3.7 2.4 2.1 1.8 1.7 2.0 2.3 2.2 2.5 2.4

• note some replacement values are affected by Stack A or D calibration data. These results are not used in subsequent Ib/lhr calculations

# ArcelorMittal Mincora Mine Pellet Plant Replacement S02 Values Stacks Band C 

# TIME STAMP 

# STACK A STACK B STACKC STACK D Results Results Results Results 

# replacemen replacemen S02Ave g 

# lS02 Average S02Average 15 min interval ppm Dry ppm Dry Avg Avg 3/21/08 1:00 6.3 4.8 3/21/081:15 5.8 4.5 3/21/08 1:30 4.9 3/21/08 1:45 5./ 3/21/082:00 4.8 3/21/082:15 4.8 3/21/082:30 3/21/082:45 3/21/083:00 3/21/083:15 3/21/083:30 3/21/08 3:45 3/21/084:00 3/21/084:15 - c-**.~--** 

# 3/21/084:30

.**-~ ~-**  

# 3/21/084:45 3/21/085:00 ---- - --.



## -- 

# 3/21/085: 15 3/21/085:30 3/21/08 5:45 I 

# 3/21/086:00 

# I 3/21/086:15 6.5 3/21/086:30 6.4 3/21/086:45 3/21/08 7:00 4.4 

# I 3/21/087:15 1.9 3/21/087:30 (9 3/21/087:45 .2 3/21/088:00 3/21/088:15 3/21/088:30 3/21/08 8:45 3/21/089:00 3/21/089:15 3/21/089:30 3/21/089:45 3/21/0810:00 3/21/0810:15 3/21/0810:30 3/21/0810:45 3/21/08 11:00 3/21/0811:15 3/21/08 11:30 3/21/08 11:45 3/21/08 12:00 3/21/0812:15 3/21/0812:30 3/21/0812:45 3/21/0813:00 3/21/0813:15 3/21/0813:30 3/21/08 13:45 3/21/0814:00 3/21/0814:15 3/21/08 14:30 3/21/08 14:45 3/21/0815:00 4.7 1.9 3/21/0815:15 5.1 2.8 3/21/0815:30 5.0 2.9 3/21/08 15:45 5.0 3/21/0816:00 3/21/0816:15 3/21/0816:30 3.3 3/21/0816:45 2.9 Barr Engineering Co. December 5. 2008

• note some replacement values are affected by Stack A or D calibration data. These results are not used in subsequent Ib/lhr calculations ArcelorMiltal Mincora Mine Pellet Plant 

# TIME STAMP

15 min interval 

# 3/21/08 1:00 

# 3/21/081:15 3/21/08 1:30 

# 3/21/08 1:45 

# 3/21/082:00 3/21/082:15 3/21/082:30 3/21/082:45 3/21/083:00 3/21/083:15 3/21/083:30 3/21/08 3:45 

# 3/21/084:00 3/21/084:15 3/21/084:30 3/21/084:45 3/21/085:00 3/21/085: 15 

# 3/21/085:30 3/21/08 5:45 1 

# 3/21/086:00 

# I 3/21/086:15 3/21/086:30 3/21/086:45 3/21/08 7:00 3/21/087:15 3/21/087:30 3/21/087:45 3/21/088:00 3/21/088:15 3/21/088:30 3/21/08 8:45 3/21/089:00 3/21/089:15 3/21/089:30 3/21/089:45 3/21/0810:00 3/21/0810:15 3/21/0810:30 3/21/0810:45 3/21/08 11 :00 

# 3/21/0811:15 3/21/08 11 :30 

# 3/21/08 11:45 

# 3/21/08 12:00 3/21/0812:15 3/21/0812:30 3/21/0812:45 3/21/0813:00 3/21/0813:15 3/21/0813:30 3/21/08 13:45 

# 3/21/0814:00 3/21/0814:15 3/21/08 14:30 3/21/08 14:45 3/21/0815:00 3/21/0815:15 3/21/0815:30 3/21/08 15:45 

# 3/21/0816:00 3/21/0816:15 3/21/0816:30 3/21/0816:45 Replacement S02 Values Stacks Band C 

# STACK A STACK B Results Results 

# repiacemen S02Average S02Average

ppm Dry ppm Dry

Avg Avg 6.3 -1.8 

# 5.8 -1.5 

# 6.2 -1.9 

# 6.4 5.1 

# 6.1 -1.8 

# 6.2 -1.8 

# 5.7 -1.-1 

# 6.3 -1.8 

# 6.1 -1.9 

# 6.5 

# 5.2 6.3 -1.9 

# 6.3 -1.7 

# 6.1 -1.7 

# 6.0 -1.6 

# ---=-JI- -1.3

.. 

## - 

# ±I i-' 

## - -- 

# 5.4 --

..

## - 

# 6.3 

# 5.2 7.2 6.1 

# 7.2 

# 6.2 6.6 

# 5.5 6.5 

# 5.5 6.4 5.1 

# 6.1 -1.6 

# STACKC STACK D Results Results 

# repiacemen .SQ2Mimjge S02Average '<) 

# .ppmQry· ppm Dry

··.····Avg>{ Avg 3.9 2.6 3.7 2.5 4.0 2.8 4.1 2.9**~jl** 

# 2.7 3.9 2.7 3.6

# ~ 3.9 2.6 3.9 2.8

# ~ 

# lQ 3.9 2.8 3.8 2.6
... __ 3.8



# . .1.§.
...... 3.7

..

## - 1,-, 

# . .l.§. _.-**-~** 

### .. 

# .l.-1.

---- 

## ---- .-



### .- 

# 4.4 j} ..

## - 

# 5.0 3.8 5.0 3.9

# ~ 

# .l.d 4.5 3.4 4.2 3.0 3.8 2.6 5.8 -1.-1 

# I 3.6 2.4 6.2 -1.9

# ~**~** 6.3 -1.9 

# 4.0 2.7 5.8 -1.2 

# 3.4 2.2 4.9 

# 3.7 

# 1.Q .2Jl 5.9 -1.6 

# 3.8 2.6 6.5 5.1 

# 4.2 2.9 6.2 -1.9 

# .5-9 2.8 6.1 

# 5.9 3.7 4.0 6.0 -1.3 

# ..l.&**~** 5.3 

# 3.9 3.2 2.1 5.6 -1.0 

# 3.2 2.0 4.7 

# 2.9 

# 'n 1,1 5.4 

# 3.7 2.8 1.7 4.9 3.-1 

# 2.6 1.7 4.4 

# 3.2 2.4 1.7 4.3 

# 3.2 2.3 1.7 4.4 

# 3.3

# ~ 

# ...1& 4.9 

# 3.6 2.5 1.9 5.8 -1.1 

# 3.0

# ~.- 5.5 

# 3.9 

# 1- 2,8 5.0 

# 3.6 2.6 1.9 .:::: 4.8 

# 3.6 2.5 1.9

-- -**~** 

# 4.6 3.-1 

# 2.4 

# .1&
__ 5.0 

# 3.6 2.5 1.8 4.7 3.-1 

# 2.4 1.8 5.5 -1.0

# ~.~ 2..1 6.0 -1.-1 

# 3.2 2.3 5.5 -1.2 

# 3.1 2.3 5.3 -1.1 

# 3.0 2.3 5.5 -1.1 

# 3.0 2.2 5.2 

# 3.8 2.8 

# .1J. 4.7 

# 3.5 2.5 1.9 5.1 

# 3.8 2.8 2.1 5.0 -1.0 

# 2.9

# ~ 5.0 

# 3.8 2.7 2.1 5.7 -1.2 

# 2.9 2.2 5.2 

# 3.9 2.8 2.1 4.4 

# 3.3 2.3 1.8 3.7 

# 2.9 2.0 1.7 Barr Engineering Co. December 5, 2008

• note some replacement values are affected by Stack A or D calibration data. These results are not used in subsequent Ib/lhr calculations

# ArcelorMittal Mincora Mine Pellet Plant Replacement S02 Values Stacks Band C 

# TIME STAMP 

# STACK A STACK B STACKC STACK D Results Results Results Results 

# replacemen replacemen S02Average S02 Average S02 Average 15 min interval 

# oOfhOrv ppm Dry ppm Dry 

# f. ,V:j 

# Avg Avg 3/21/08 17:00 

# .1 1.8 3/21108 17:15 1.9 3/21/0817:30 2.0 3/21/0817:45 2.1 3/21/08 18:00 2.0 3/21/0818:15 2.1 3/21/08 18:30 2.8 3/21/0818:45 3.7 2.9 3/21/0819:00 3.9 3.0 3/21/0819:15 6.3 

# 5.1 3.9 3.0 3/21/0819:30 4. 

# 3.7 3/21/0819:45 3.5 3/21/0820:00 3/21/0820:15 3/21/0820:30 3/21/0820:45 3/21/0821 :00 3/21/0821:15 3/21/0821:30 3/21/0821:45 3/21/0822:00

_. 

# 3/21/0822: 15 3/21/0822:30 3/21/0822:45 

# I 3/21/0823:00 3/21/08 23:15 3/21/0823:30 4.4 

# 3/21/0823:45 !.4 

# 3/22108 0:00 .7 

# 3/221080:15 3/22108 0:30 3/22108 0:45 3/22108 1:00 3.8 

# 3/221081:15 4.0 

# 3/22108 1:30 3.9 

# 3/22108 1:45 3.7 

# 3/22108 2:00 3.8 

# 3/221082:15 3.7 

# 3/22108 2:30 4.0 

# 3/22108 2:45 4.0 

# 3/22108 3:00 3.8 

# 3/22108 3:15 3.1 

# 3/22108 3:30 3/22108 3:45 3/22108 4:00 3/221084:15 E 

# 3/22108 4:30 3/22108 4:45 3/22108 5:00 3/22/085:15 

# >1 3/22108 5:30 

# 1.5

-- 

# 3/22108 5:45

- 

# .2
-. 

# ----, c_ .

__ ._ 

# 3/22108 6:00 .7

---- 

# 3/221086:15 '.9 

# 3/22108 6:30 3/22108 6:45

--- 

# 3/22108 7:00 3/221087:15 3/22108 7:30 -I. 

# 3/22108 7:45 

# 5.. 3/221088:00 7.1 

# Barr Engineering Co. December 5, 2008

* note some replacement values are affected by Stack A or D calibration data. These results are not used in subsequent Ibllhr calculations ArcelorMittal Mincora Mine Pellet Plant

_. 

# TIME STAMP

15 min interval 

# 3/21/0B 17:00 3/2110B 17:15 3/21/0B 17:30 3/21/0B 17:45 3/21/0B 1B:00 3/21/0B 1B:15 3/2110B 1B:30 3/21/0B 1B:45 3/21/0B 19:00 3/21/0B 19:15 3/21/0B 19:30 3/21/0B 19:45 3/21/0B 20:00 3/21/0B 20:15 3/21/0B 20:30 3/21/0B 20:45 3/21/0B 21 :00 

# 3/21/0B 21:15 3/21/0B 21:30 3/21/0B 21:45 3/21/0B 22:00 3/21/0B 22: 15 

# 3/21/0B 22:30 3/21/0B 22:45 

# I 3/21/0B 23:00 3/21/0B 23: 15 

# 3/21/0B 23:30 3/21/0B 23:45 3/2210B 0: 00 

# 3/2210B 0:15 3/2210B 0:30 3/2210B 0:45 3/2210B 1 :00 

# 3/2210B 1:15 

# 3/22108 1 :30 

# 3/2210B 1 :45 

# 3/22108 2:00 3/221082:15 3/22108 2:30 3/2210B 2:45 3/2210B 3:00 3/22108 3: 15 

# 3/22108 3:30 3/22108 3:45 3/22108 4:00 3/221084:15 3/2210B 4:30 3/2210B 4:45 3/2210B 5:00 3/22/085:15 3/22108 5:30 3/2210B 5:45 3/22108 6:00 3/221086:15 3/22108 6:30 3/2210B 6:45 3/2210B 7:00 3/2210B 7: 15 

# 3/22108 7:30 3/22108 7:45 3/221088:00 Replacement S02 Values Stacks Band C 

# STACK A STACK B Results Results 

# replacemen S02Average S02 Average

ppm Dry ppm Dry

Avg Avg 4.0 3.1 4.5 3.-1 5.1 3.7 5.2 3.9 4.9 3.7 5.2 3.9 5.7 -1.7 6.0 -1.9 6.3 5.0 

# 6.3 5.1 6.2 -1.9 6.0 -1.6 5.5 -1.2 6.4 5.3 6.9 5.7 6.7 5.6 

# 6.B 5.8 6.3 5.2 6.1 5.1 6.3 5.3 6.1 5.2
...._ 6.2

.. 

## - - 

# _5J.
__ 6.1**i~** 

# 6.0 -1.9 6.3 5.1 6.2 -1.8 

# 5.B -1.-1 

# 5.B -1.-1 5.9 -1.7 6.4 5.2 6.6 5.5 6.0 5.1 6.1 5.2 6.1 5.5 6.1 -1.9 6.1 5.3 6.3 5.5 6.0 5.3 6.4 5.8 6.4 5.8 6.3 5.-1 5.6 -1.-1 4.9 -1.0 

# 5.0 -1.1 4.9 -1.1 6.0 -1.8 5.2 -1.3 4.9 3.9 4.6 3.7 5.5 -1.-1 5.7 -1.5 5.4 -1.2
...... 4.8

# +~ 5.0 

# _. 5.5 -1.-1**~-** 

# 5.5 -1.6 6.2·--- .. 

# 5.3 

# ._ .. 

# 6.0 5.2 5.2 -1.9 5.7 5.1 6.2 7.0 

# Barr Engineering Co. December 5, 

# 200B 

# STACKC STACK D Results Results 

# replacemen $02 Average S02 Average

ppm

# Dry ppm Dry

Avg·/ Avg 2.2 

# 1.B 2.5 1.9 

# 2.B 2.0 2.9 2.1 

# 2.B 2.0 3.0 2.1 3.7 

# 2.B 3.7 2.9 3.9 3.0 3.9 3.0 3.7 

# 2.B 3.5 2.5 3.2 2.4 4.1 3.2 4.4 3.5 4.1 3.4 4.2 3.5- 

# 3.B 3.2--- 3.7 3.1 

# 3.B 3.2 3.7 3.2 .- 

# 3.B 3.3 3.5 3.0

. ...... 

# 3.5 2.9

# .~}.- 3.1 2.6

...... 

# 3.2 2.4 3.2 2.4 3.4 2.7 

# 3.B 3.1 4.0 3.3 3.7 3.1 3.8 3.3 4.0 3.6 3.9 

# 2.B 3.7 3.4 3.8 3.4 3.7 3.4 4.0 3.7 4.0 3.9 

# 3.B 3.4 3.1 2.5 2.8 2.3 2.9 2.4 2.9 2.5 3.4 

# 2.B 3.0 2.5 2.7 2.2 2.6 2.2 3.2 2.6 3.2

# .~§ -- 

# .._-*_
...

---**~** 

# 2.8-

....

## - 1- 

# 3.1 3.3**~--** 

# "H
_ ... 3.8 3.7 3.3 3.7 3.3 3.6 3.3 5.2 5.3

* note some replacement values are affected by Stack A or D calibration data. These results are not used in subsequent Ibllhr calculations

# Method Used for 

# S02 Data Replacement ArcelorMittal Minorca Mine Furnace Line Waste Gas S02 Testing Estimated values were used during times of invalid data on stacks B and C. These values were generated by determining the relationship between stacks [Ex: (BID), (BI

# A), (CID), 

# and (CIA)] 

# during times of valid data. Using these relationships we extrapolated values for Band C based on A and D independently. These values were averaged to determine our estimate. The complete data set, including estimated data, was graphed to determine accuracy of the representation. 

# Method Used for 

# S02 Data Replacement ArcelorMittal Minorca Mine Furnace Line Waste Gas S02 Testing Estimated values were used during times of invalid data on stacks B and C. These values were generated by determining the relationship between stacks [Ex: (BID), (BI 

# A), (CID), 

# and (CIA)] 

# during times of valid data. Using these relationships we extrapolated values for Band C based on A and D independently. These values were averaged to determine our estimate. The complete data set, including estimated data, was graphed to determine accuracy of the representation.

## --- 

# --_._ - -- - _. 

# 502 

# Concentration**~~-- ---** **-~**



# 9

-- --_ .. 

# f**St ~ck** **-A** 

# 10

- ,-- - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - ----; - Stack B

- Stack B repl Stack C

-**-~** 

# - --. - - - .- . -- Stack C repl

- Stack D 

# 8

- I--.,--- t----:--------- + ----



# 2 

# 6

- -

1 

# 7
. - - --- ---- - - .. --- - --- - .. -- . -**-~** 

# -_.

E ll. ll. (I) 

## Ol 

# 5 · - . > 

# <t 

# o lJ)



# Replacementdata for portions of stacks Band C are flagged with a diamond symbol 

# 650 600 550 500 450 400 Data Point



# - - - - - _.- 

# 300 350 250 200 150 100 50 

# o**L- ----;-** **---'- -;---** **--:- ---!** **=r== ==:!...-** **~--~- -=** **=- ....,___** **__;_ ----** **__r --** **__r__ -=** **=l** 

# o 

# I L.

_ _ . • •**~~** _ 

# E Il. Il. CIl 

## 01 ('G

# ~ 

# > 

# <t 

# 0 (/)



# i 

# I -- - - -- --

_ ._ ._- -------- - - - 

# S02 Concentration --Stack A 

# 10**.--------------------------------------------- ---** **------- --** **----------------- ---** **StackB**



# - Stack B repl Stack C 

# 9 8 7 

# 6 5 4 

# 3 Stack C repl

-- - Stack D



# 2**'--I~ l-1H~H-I'**  

# -. - -------- 

# 1

--- -- - --- -- ------ . ------- --- -- --- '\.N\If lJ 

# Replacement data for portions of stacks B and C are flagged with a diamond symbol 

# o o 50 100 150 200 250 300 350 400 450 500 550 600 650 Data Point 

# "--------------------

- ---- --.-

# AppendixB Field Data Sheets 

# AppendixB Field Data Sheets

# BARR Engineering Company EPA METHOD 6C 50 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mitlal7-day Nox CEMS Furnace Scrubber Stack A-D 

# 3/11/08 P. Rossmiller Cylinder Serial No. Certified Value Zero Gas CC176437 0.0 Low-rance

Mid-ranCle CC238857 18.4 Hiqh-ranqe CC68268 48
ANALYZER CALIBRATION DATA (Initial 

# 3/11/08) Note: Difference must be less than 

# +1- 2 percent of span Stack A - S02(1) Analyzer Analyzer Mod 

# 1 SN 100AH Cylinder Value Calibration Absolute Difference as Analyzer Span: 48 Response Difference % of Span Zero Gas 0 0.2 0.2 0.42% Low- Rance Mid - Range 18.4 18.3 0.1 0.21% High - Range 48 47.9 0.06 0.13% Stack B - S02(2) Analyzer Analyzer Mod 

# 1 SN 100EH Cylinder Value Calibration Absolute Difference as Analyzer Span: 48 Response Difference % of Span Zero Gas 0 0.1 0.1 0.21% Low- Range Mid - Range 18.4 18.8 0.4 0.83% High - Range 48 47.8 0.2 0.42% Stack C - S02(3) Analyzer Analyzer Mod 

# 1 SN 100AH Cylinder Value Calibration Absolute Difference as Analyzer Span: 48 Response Difference % of Span Zero Gas 0 0.0 0 0.00% Low- Ranqe Mid - Range 18.4 18.8 0.4 0.83% High - Range 48 47.7 0.3 0.62% Stack D - S02(4) Analyzer Analyzer Mod 

# 1 SN 100AH Cylinder Value Calibration Absolute Difference as Analyzer Span: 48 Response Difference % of Span Zero Gas 0 0.1 0.1 0.21% Low- Rance Mid - Range 18.4 19.0 0.6 1.25% High - Range 48 48.2 0.2 0.42% SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span Initial Values Final Values 'WHI! 

## (iU.!3.!i08MWWLLi rifi\PM,riitii: Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK A (1) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 107 0.0 0.2 0.7 1.00% 0.3 0.21% -0.79% Upscale Gas 104 18.4 18.3 17.3 -2.02% 18.5 0.42% 2.44%
Initial Values Final Values itil iLrllVr WHis ifam 

## iPM, 

# iiiii Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK B (2) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 98 0.0 0.1 1.2 2.29% 0.9 1.67% -0.63% Upscale Gas 96 18.4 18.80 19.4 1.19% 19.0 0.42% -0.77%
Initial Values Final Values 

# ii!f! iiiiii! iiAiVi/4! !Ji'!fi§PMiiWiti!ii; Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACKC (3) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 103 0.0 0.1 0.6 0.98% 1.8 3.54% 2.56% Upscale Gas 108 18.4 18.8 19.4 1.19% 21.6 5.88% 4.69%
Initial Values Final Values 

# !!@W;;;;; jjif 

## WW;piViW/;!/i/i Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACKD (4) Time (sec) PPM PPM PPM % of Soan PPM % of Span span Zero Gas 90 0.0 0.1 0.5 0.77% 1.4 2.62% 1.85% Upscale Gas 88 18.4 19.0 19.3 0.69% 19.1 0.21% -0.48% System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span] x 100 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-range High-range Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 

# 3/11/08 P. Rossmiller Cylinder Serial No. CC176437 CC238857 CC68268
ANALYZER CALIBRATION DATA (Initial 

# 3/11/08) Certified Value 0.0 18.4 48

Note: Difference must be less than 

# +1- 2 percent of span Stack A - S02(1) Analyzer Analyzer Mod 

# I SN 100AH Cylinder Value Calibration Analyzer Span: 48 Response Zero Gas 0 0.2 Low- Range Mid - Range 18.4 18.3 High - Range 48 47.9 Stack B - S02(2) Analyzer Analyzer Mod 

# I SN 100EH Cylinder Value Calibration Analyzer Span: 48 Response Zero Gas 0 0.1 Low- Range Mid - Range 18.4 18.8 High - Range 48 47.8 Stack C - S02(3) Analyzer Analyzer Mod 

# I SN 100AH Cylinder Value Calibration Analyzer Span: 48 Response Zero Gas 0 0.0 Low- Range Mid - Range 18.4 18.8 High - Range 48 47.7 Stack 0 - S02(4) Analyzer Analyzer Mod 

# I SN 100AH Cylinder Value Calibration Analyzer Span: 48 Response Zero Gas 0 0.1 Low- Range Mid - Range 18.4 19.0 High - Range 48 48.2 Absolute Difference 0.2 0.1 0.06
Absolute Difference 0.1 0.4 0.2
Absolute Difference 0 0.4 0.3
Absolute Difference 0.1 0.6 0.2 

# EPA METHOD 6C 50 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span Initial Values Final Values Difference as 

# 3/11/2008 ·.AM 

# 3/11/2008. 

# .. PM

% of Span Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias 0.42% STACK A (1) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 107 0.0 0.2 0.7 1.00% 0.3 0.21% 0.21% Upscale Gas 104 18.4 18.3 17.3 -2.02% 18.5 0.42% 0.13% Initial Values Final Values Difference as 

# 3/11/2008 AM 

# 3/11/2008 PM % of Span Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias 0.21% STACK B (2) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 98 0.0 0.1 1.2 2.29% 0.9 1.67% 0.83% Upscale Gas 96 18.4 18.80 19.4 1.19% 19.0 0.42% 0.42% Initial Values Final Values Difference as 

# 3/11/2008 •... 

# AM 

# 3/11/2008 PM % of Span Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias 0.00% STACKC (3) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 103 0.0 0.1 0.6 0.98% 1.8 3.54% 0.83% Upscale Gas 108 18.4 18.8 19.4 1.19% 21.6 5.88% 0.62% Initial Values Final Values Difference as 

# 31.11/2008. AM 

# 3/11/2008 PM 

# ••

% of Span Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias 0.21% STACK 0 (4) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 90 0.0 0.1 0.5 0.77% 1.4 2.62% 1.25% Upscale Gas 88 18.4 19.0 19.3 0,69% 19.1 0.21% 0.42% System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# I Span] x 100 Drift, Percent of

span -0.79% 2.44%

Drift, Percent of

span -0.63% -0.77%

Drift, Percent of

span 2.56% 4.69%

Drift, Percent of

span 1.85% -0.48%

# BARR Engineering Company EPA METHOD 6C 50 2 

# CEM5 ANALYZER CALIBRATION Project Sample Loc. Date Operators Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 

# 3/11/08 P. Rossmiller Cvlinder Serial No. Certified Value Zero Gas CC176437 0.0 Low-rance

Mid-ranqe CC238857 18.4 

# Hiqh-ranqe CC68268 48
ANALYZER CALIBRATION DATA (Analyzer Cal 

# 3/11108 AM) Note: Difference must be less than 

# +1- 2 percent of span SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span

System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# I Span] x 100 Initial Values Final Values 

# "",JifiJii}'!'i!/f/fY0i: i!J!d,: i!i)(iJiN@i!jiJUhWJU; 

## Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response. Cal. Bias Percent of STACKB (2) Time (sec) PPM PPM PPM % of Soan PPM % of Soan soan Zero Gas 98 0.0 0.1 0.9 1.67% 1.1 2.08% 0.42% Upscale Gas 96 18.4 18.80 19.0 0.42% 18.4 -0.83% -1.25% Initial Values Final Values 

# iJiiYiliiii,Uiiii DY,Y 

# W1iWJWiiJiti

# ii0JJlii Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response. Cal. Bias Response, Cal. Bias Percent of STACK A (1) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 107 0.0 0.2 0.3 0.21% 0.9 1.46% 1.25% Upscale Gas 104 18.4 18.3 18.5 0.42% 18.3 0.00% -0.42%

Initial Values Final Values**,;~** 

### ii)iii 

# N/f!i';0"iiW.Viii )iiiii, 

## Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response. Cal. Bias Response, Cal. Bias Percent of STACKC (3) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 103 0.0 0.1 1.8 3.54% 3.1 6.25% 2.71% Upscale Gas 108 18.4 18.8 21.6 5.88% 21.8 6.25% 0.37%
Initial Values Final Values 

# ,Jki.w!!!WMiffii!i)J! 

# iiPi!!' ;WiWiiiiiiiJ!J'$i!YY'iiiii:i Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response. Cal. Bias Percent of STACK D (4) Time (sec) PPM PPM PPM % of Span PPM % of Span soan Zero Gas 90 0.0 0.1 1.4 2.62% 0.7 1.25% -1.37% Upscale Gas 88 18.4 19.0 19.1 0.21% 19.4 0.83% 0.62%



# - 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-range High-range Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 

# 3/11/08 P. Rossmiller Cylinder Serial No. CC176437 CC238857 CC68268 Certified Value 0.0 18.4 48
ANALYZER CALIBRATION DATA (Analyzer Cal 

# 3/11108 AM) Note: Difference must be less than 

# +1- 2 percent of span .' 

# ..•. SICjckA-S02(j) 

# .... 

# · Anlliyzer '.' A[1alyze( ModI. SN 100AH CylinderVah.lE! Analyzer Span: '.' "48< Call9ratio[1. Response' 

# 1>< 

# ....... '; 

# .1'.,

. 

# ..... .. •Zero Gas 

# .. ' .. 

# .... I 0 • 

# . i:J.2 .'



# .....**Low~Range** 

# '
.. '
..'. ". :)i 

# O' 

# . ..• 

# ..

.. 

# Mld·.Raf)ge 

# : 18.4 

# ....... • ." .18;3 .' High -Range :: 

# 48 ' 

## :., 

# 47.9



# . : . ". 

## : 

# . .. : .,: 

# • . "Stack. B- S02(2) 

# . •••••••••• 

# Analyzer •• Analyzer ModI SN 100EH 

# I." CylinqerValue. Analyzer Span, 

# 48
... Calibration



# ........ 

# ' Re S P9 n SEi!;



# ..... "ZeroGas I. '0 : j •• 

# 0:1 ;



## .... 

# Low., Range:**~""** 

# .'.: 

# '<Q .. '



# .. ··:.Mld 

# c .Range 

# " 

# . ,'. 18.4. ....• 

# . ... 

# 18:8 ;. 

# •.... High; Range 

# ....... 

# I···· " . 48 . ·47.8.: 

# . ' 

### .' 

# .

Absolute Difference


# .

.....

0.2 0.0 i 

# '0;1 0.06

' 

# . Absolute

Difference 0.1 

# .. : 

# 0;0 0.4 " 

# . :.0.2 '-'"- " 

# .'.
.... 

# .... Stack 

# c- S02(3) 

# .... " 

# Analyzer 

# . Analyzer Mod/.SN 100AH 

# ..... 'Absolute Cylinder Value Calibration Analyzer $pan: 48 

# . Response Difference



# . :' 

## : 

# ZerbGas 0 

# .' .: 

# 0.0 

# . O. Low-;Range 

# .... : 

# 0 

# '. 

# · 0.0**Mid~Range** 

# '. :18.4 ". 

# 18.8 0.4 High**.~.** 

# Range / 

# .... 48 :." , 

# 47.7 0.3 '.' 

# .... : 

# EPA METHOD 6C 50 2 

# CEM5 ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span Initial Values Final Values Difference as. 

# 3/11/2008 '.' 

# 3/11/2008 '.'



# % of Sparr '. Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response. Cal. Bias Response, Cal. Bias .\ 

# 0.42% ". 

# STACK A (1) Time (sec) PPM PPM PPM % of Span PPM % of Span 0,00% Zero Gas 107 0.0 0.2 0.3 0.21% 0.9 1.46% 0.21% Upscale Gas 104 18.4 18.3 18.5 0.42% 18.3 0.00% 0;13% Initial Values Final Values Difference as 

# 3/11/2008 

# . 311112008

%of$pan Cylinder Analyzer Cal System Cal System Cal System Cal System Cal 

# .. .. 

# Response Value Response, Response, Cal. Bias Response, Cal. Bias 0
.. 21% STACKB (2) Time (sec) PPM PPM PPM % of Span PPM % of Span
'.' 

# 0,00% Zero Gas 98 0.0 0.1 0.9 1.67% 1.1 2.08% 0.83% Upscale Gas 96 18.4 18.80 19.0 0.42% 18.4 -0.83% 0.42% Initial Values Final Values Difference as 

# 3/11/2008 .' 

# 3/11/2008

% of Span Cylinder Analyzer Cal System Cal System Cal System Cal System Cal .' 

# Response Value Response, Response. Cal. Bias Response, Cal. Bias 0.00% STACK C (3) Time (sect PPM PPM PPM % of Span PPM % of Span 0.00% Zero Gas 103 0.0 0.1 1.8 3.54% 3.1 6.25% 0.83% Upscale Gas 108 18.4 18.8 21.6 5.88% 21.8 6.25% 0.62% Initial Values Final Values 

# 3/11/2008 

# . ' 

## . 

# 3/11/2008 .'. 

## , 

# Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias STACK D (4) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 90 0.0 0.1 1.4 2.62% 0.7 1.25% Upscale Gas 88 18.4 19.0 19.1 0.21% 19.4 0.83%



# - System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# I Span] x 100 Drift, Percent of

span 1.25% -0.42%

Drift, Percent of

span 0.42% -1.25%

Drift, Percent of

span 2.71% 0.37%

Drift, Percent of

span -1.37% 0.62%

# BARR Engineering Company EPA METHOD 6C 50 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/11/2008 - 3/12/08

P. Rossmiller 

# Cvlinder Serial No. Certified Value Zero Gas CC176437 0.0 tow-ranee

Mid-ranqe CC238857 18.4 High-range CC68268 48
ANALYZER CALIBRATION DATA Note: Difference must be less than +/- 2 percent of span

Rezero and span analyzer Stack C - S02(3) Analyzer Analyzer Mod / SN 100AH Cylinder Value Calibration Absolute Difference as Analyzer Span: 48 Response Difference % of Span Zero Gas 0 0.0 0 0.00% Low- Range 0 0.0 0.00% Mid - Range 18.4 18.8 0.4 0.83% High - Range 48 48.8 0.8 1.67% SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed +/- 5 percent of span. Drift cannot exceed +/- 7.5 percent of span Initial Values Final Values 3/1'1/2008 3/12/2008 1207 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response. Cal. Bias Percent of STACK A (1) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 107 0.0 0.2 0.9 1.46% 1.4 2.50% 1.04% Upscale Gas 104 18.4 18,3 18.3 0.00% 18.9 1.25% 1.25%
Initial Values Final Values 3/11/2008 3/12/2008 12189 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK B (2) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 98 0.0 0.1 1.1 2.08% 1.2 2.29% 0.21% Upscale Gas 96 18.4 18.80 18.4 -0.83% 19.0 0.42% 1.25%
Initial Values Final Values 3/11/2008 3/12/2008 1237 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACKC (3) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 103 0.0 0.0 0.0 0.04% -0.8 -1.67% -1.71% Upscale Gas 108 18.4 18.8 18.6 -0.42% 19.0 0.42% 0.83%
Initial Values Final Values 3/11/2008 3/12/2008 1247 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK D (4) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 90 0.0 0 0.7 1.46% 0.7 1.46% 0.00% Upscale Gas 88 18.4 19.0 19.1 0.21% 19.4 0.83% 0.62% System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) / Span] x 100 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-range High-range Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/11/2008 - 3/12/08



# P. Rossmiller Cylinder Serial No. CC176437 CC238857 CC68268
ANALYZER CALIBRATION DATA Certified Value 0.0 18.4 48

Note: Difference must be less than 

# +1- 2 percent of span
..•,. Slack A

# ~S02(1) Analy?er**~odl** 

# SN 100AH Analyzer Span:

Rezero and span analyzer Stack C - S02(3) Analyzer Analyzer Mod 

# 1 SN 100AH Cylinder Value Calibration Analyzer Span: 48 Response Zero Gas 0 0.0 Low- Range 0 Mid - Range 18.4 18.8 High - Range 48 48.8 StackD - S02(4) i\nalyzer Modi SN 100AH Am:ilY2er Span; 48 Absolute Difference 0 0.0 0.4 0.8 

# EPA METHOD 6C 50 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span Initial Values Final Values 3/1'112008 3/12/2008 

# 1207 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias STACKA(1) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 107 0.0 0.2 0.9 1.46% 1.4 2.50% Upscale Gas 104 18.4 18,3 18.3 0.00% 18.9 1.25%
Initial Values Final Values 3/11/2008 3/12/2008 

# 12189 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias STACK B (2) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 98 0.0 0.1 1.1 2.08% 1.2 2.29% Upscale Gas 96 18.4 18.80 18.4 -0.83% 19.0 0.42%
Initial Values Final Values Difference as 3/11/2008 3/12/2008 

# 1237

% of Span Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias 0.00% STACKC_(3) Time (sec) PPM PPM PPM % of Span PPM % of Span 0.00% Zero Gas 103 0.0 0.0 0.0 0.04% -0.8 -1.67% 0.83% Upscale Gas 108 18.4 18.8 18.6 -0.42% 19.0 0.42% 1.67% Initial Values Final Values 3/11/2008 3/12/2008 

# 1247 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias STACK D (4) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 90 0.0 0 0.7 1.46% 0.7 1.46% 1.25% Upscale Gas 88 18.4 19.0 19.1 0.21% 19.4 0.83% 0.42% System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span] x 100 Drift, Percent of

span 1.04% 1.25%

Drift, Percent of

span 0.21% 1.25%

Drift, Percent of

span -1.71% 0.83%

Drift, Percent of

span 0.00% 0.62%

# BARR Engineering Company EPA METHOD 6C 50 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/12/08 P. Rossmiller Cylinder Serial No. Certified Value Zero Gas CC176437 0.0 Low-rance

Mid-ranQe CC238857 18.4 

# Hioh-rance CC68268 48
ANALYZER CALIBRATION DATA Note: Difference must be less than 

# +/- 2 percent of span SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

## +/- 5 percent of span. Drift cannot exceed 

## +/- 7.5 percent of span Stack A - S02(1) Analyzer Analyzer Mod / SN 100AH Cylinder Value Calibration Absolute Difference as Analyzer Span: 48 Response Difference % of Span Zero Gas 0 0.2 0.2 0.42% Low- Rance 0 0.0 0.00% Mid - Range 18.4 18.3 .0.1 0.21% High - Range 48 47.9 0.06 0.13% Initial Values Final Values 3/12/2008 1207 3/12/2008 2303 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift. Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK A (1) Time (sec) PPM PPM PPM % of Soan PPM % of Soan span Zero Gas 107 0.0 0.2 1.4 2.50% 0.0 -0.42% -2.92% Upscale Gas 104 18.4 18.3 18.9 1.25% 18.9 1.25% 0.00%
Stack B - S02(2) Analyzer Analyzer Mod / SN 100EH Cylinder Value Calibration Absolute Difference as Analyzer Span: 48 Response Difference % of Span Zero Gas 0 0.1 0.1 0.21% Low- Ranoe 0 0.0 0.00% Mid - Range 18.4 18.8 0.4 0.83% High - Range 48 47.8 0.2 0.42% Initial Values Final Values 3/12/2008 1218 3/12/2008 2255 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response. Response, Cal. Bias Response. Cal. Bias Percent of STACK B (2) Time (sec) PPM PPM PPM % of Soan PPM % of Soan soan Zero Gas 98 0.0 0.1 1.2

# 2.29o)~ -0.6 -1.46% -3.75% Upscale Gas 96 18.4 18.80 19.0 0.42% 19.1 0.63% 0.21%
Stack C - S02(3) Analyzer Analyzer Mod / SN 100AH Cylinder Value Calibration Absolute Difference as Analyzer Span: 48 Response Difference % of Span Zero Gas 0 0.0 0 0.00% Low- Range 0 0.0 0.00% Mid - Range 18.4 18.8 0.4 0.83% High - Range 48 48.8 0.8 1.67% Initial Values Final Values 3/12/2008 1237 3/12/2008 2248 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response. Cal. Bias Percent of STACKC (3) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 103 0.0 0.0 -0.8 -1.67% 0.1 0.21% 1.88% Upscale Gas 108 18.4 18.8 19.0 0.42% 18.5 -0.63% -1.04%



# 502 

## System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) / Span] x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) / Span] x 100 Initial Values Final Values 3/12/2008 1247 3/12/2008 2259 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK D (4) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 90 0.0 0 0.7 1.46% 0.8 1.67% 0.21% Upscale Gas 88 18.4 19.0 19.4 0.83% 19.1 0.21% -0.62%



# - Stack D - S02(4) Analyzer Analyzer Mod / SN 100AH Cylinder Value Calibration Absolute Difference as Analyzer Span: 48 Response Difference % of Span Zero Gas 0 0.1 0.1 0.21% Low- Rance 0 0.0 0.00% Mid - Range 18.4 19.0 0.6 1.25% High - Range 48 48.2 0.2 0.42% 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-range High-range Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 

# 3/12/08 P. Rossmiller Cylinder Serial No. CC176437 CC238857 CC68268
ANALYZER CALIBRATION DATA Certified Value 0.0 18.4 48

Note: Difference must be less than 

# +1- 2 percent of span Stack A - S02(1) Analyzer Analyzer Mod 

# 1 SN 100AH Cylinder Value Calibration Analyzer Span: 48 Response Zero Gas 0 0.2 Low- Range 0 Mid - Range 18.4 18.3 High - Range 48 47.9 Stack B - S02(2) Analyzer Analyzer Mod 

# 1 SN 100EH Cylinder Value Calibration Analyzer Span: 48 Response Zero Gas 0 0.1 Low- Range 0 Mid - Range 18.4 18.8 High - Range 48 47.8 Stack C - S02(3) Analyzer Analyzer Mod 

# 1 SN 100AH Cylinder Value Calibration Analyzer Span: 48 Response Zero Gas 0 0.0 Low- Range 0 Mid - Range 18.4 18.8 High - Range 48 48.8 Stack D - S02(4) Analyzer Analyzer Mod 

# 1 SN 100AH Cylinder Value Calibration Analyzer Span: 48 Response Zero Gas 0 0.1 Low- Range 0 Mid - Range 18.4 19.0 High - Range 48 48.2 Absolute Difference 0.2 0.0 0.1 0.06
Absolute Difference 0.1 0.0 0.4 0.2
Absolute Difference 0 0.0 0.4 0.8
Absolute Difference 0.1 0.0 0.6 0.2 

# EPA METHOD 6C 50 2 

# CEMS ANALYZER CALIBRATION

Difference as

% of Span

0.42% 0.00% 0.21% 0.13%
Difference as

% of Span

0.21% 0.00% 0.83% 0.42%
Difference as % of Span

0.00% 0.00% 0.83% 1.67%
Difference as % of Span

0.21% 0.00% 1.25% 0.42% SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span Initial Values Final Values 

# 3/12/2008 1207 

# 3/12/2008 2303 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias STACK A (1) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 107 0.0 0.2 1.4 2.50% 0.0 -0.42% Upscale Gas 104 18.4 18.3 18.9 1.25% 18.9 1.25%
Initial Values Final Values 

# 3/12/2008 1218 

# 3/12/2008 2255 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response. Response, Cal. Bias Response, Cal. Bias STACK B (2) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 98 0.0 0.1 1.2 2.29% -0.6 -1.46% Upscale Gas 96 18.4 18.80 19.0 0.42% 19.1 0.63%
Initial Values Final Values 

# 3/12/2008 1237 

# 3/12/2008 2248 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias STACKC (3) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 103 0.0 0.0 -0.8 -1.67% 0.1 0.21% Upscale Gas 108 18.4 18.8 19.0 0.42% 18.5 -0.63%
Initial Values Final Values 

# 3/12/2008 1247 

# 3/12/2008 2259 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias STACK D (4) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 90 0.0 0 0.7 1.46% 0.8 1.67% Upscale Gas 88 18.4 19.0 19.4 0.83% 19.1 0.21%



# - System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span] x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) 

# 1 Span] x 100 

# 502 

# Drift, Percent of

span -2.92% 0.00%

Drift, Percent of

span -3.75% 0.21%

Drift, Percent of

span 1.88% -1.04%

Drift, Percent of

span 0.21% -0.62%

# BARR Engineering Company EPA METHOD 6C S02 CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mittal 7-day Nox CEMS Furnace Scrubber Stack A-D 3/12-13/2008 

# P. Rossmiller Cylinder Serial No. Certified Value Zero Gas CC176437 0.0 Low-range

Mid-range CC238857 18.4 High-range CC68268 48
ANALYZER CALIBRATION DATA Note: Difference must be less than 

# +1- 2 percent of span SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span

Initial Values Final Values 3/12/2008 

# 2248 3/13/2008 

# 1114 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACKC (3) Time (sec) PPM PPM PPM % of Soan PPM % of Span span Zero Gas 103 0.0 0.0 0.1 0.21% 0.0 0.00% -0.21% Upscale Gas 108 18.4 18.8 18.5 -0.63% 18.2 -1.25% -0.63% Initial Values Final Values 3/12/2008 

# 2255 3/13/2008 

# 1056 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK B (2) Time (sec) PPM PPM PPM % of Soan PPM % of Soan span Zero Gas 98 0.0 0.1 -0.6 -1.46% 1.4 2.71% 4.17% Upscale Gas 96 18.4 18.80 19.1 0.63% 18.9 0.21% -0.42% Initial Values Final Values 3/12/2008 

# 2303 3/13/2008 

# 1043 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK A (1) Time (sec) PPM PPM PPM % of Soan PPM % of Span span Zero Gas 107 0.0 0.2 0.0 -0.42% 1.6 2.92% 3.33% Upscale Gas 104 18.4 18.3 18.9 1.25% 19.3 2.08% 0.83%



# S02 System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span] x 100 Drift 

# = [(Final System Cal. Response -Initial System Cal Response) 

# 1 Span] x 100 Initial Values Final Values 3/12/2008 

# 2259 3/13/2008 

# 1129 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK 0 (4) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 90 0.0 0 0.8 1.67% 2.1 4.38% 2.71% Upscale Gas 88 18.4 19.0 19.1 0.21% 19.7 1.46% 1.25%



# - 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-range High-range Mittal 7 -day Nox CEMS Furnace Scrubber Stack A-D 3/12-13/2008 

# P. Rossmiller Cylinder Serial No. CC176437 CC238857 CC68268
ANALYZER CALIBRATION DATA Certified Value 0.0 18.4 48

Note: Difference must be less than 

# +1- 2 percent of span**St<lckA~** 

# S02(1) Analyzer Mod iSN ·100AH Analyzer .Span;

18.4 19.0 48 48.2 

# EPA METHOD 6C S02 CEMS ANALYZER CALIBRATION

1.25% 0.42% SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span Initial Values Final Values 3/12/2008 

# 2303 3/13/2008 

# 1043 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias STACK A (1) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 107 0.0 0.2 0.0 -0.42% 1.6 2.92% Upscale Gas 104 18.4 18.3 18.9 1.25% 19.3 2.08%
Initial Values Final Values 3/12/2008 

# 2255 3/13/2008 

# 1056 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias STACK B (2) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 98 0.0 0.1 -0.6 -1.46% 1.4 2.71% Upscale Gas 96 18.4 18.80 19.1 0.63% 18.9 0.21%
Initial Values Final Values 3/12/2008 

# 2248 3/13/2008 

# 1114 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response. Response, Cal. Bias Response, Cal. Bias STACKC (3) Time {sec:L PPM PPM PPM % of Span PPM % of Span Zero Gas 103 0.0 0.0 0.1 0.21% 0.0 0.00% Upscale Gas 108 18.4 18.8 18.5 -0.63% 18.2 -1.25%
Initial Values Final Values 3/12/2008 

# 2259 3/13/2008 

# 1129 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias STACK 0 (4) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 90 0.0 0 0.8 1.67% 2.1 4,38% Upscale Gas 88 18.4 19.0 19.1 0.21% 19.7 1.46%



# - System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span] x 100 Drift 

# = [(Final System Cal. Response -Initial System Cal Response) 

# 1 Span] x 100 

# S02 Drift, Percent of

span 3.33% 0.83%

Drift, Percent of

span 4.17% -0.42%

Drift, Percent of

span -0.21% -0.63%

Drift, Percent of

span 2.71% 1.25%

# BARR Engineering Company EPA METHOD 6C 50 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mitlal7-day Nox CEMS Furnace Scrubber Stack A-D 3/13-14/2008 P. Rossmiller Cylinder Serial No. Certified Value Zero Gas CC176437 0.0 

# Low-rance

Mid-ranqe CC238857 18.4 Hiqh-ranqe CC68268 48
ANALYZER CALIBRATION DATA Note: Difference must be less than 

# +/- 2 percent of span SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +/- 5 percent of span. Drift cannot exceed 

# +/- 7.5 percent of span

Initial Values Final Values 3/13/2008 1056 3114/2008 724 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift. Response Value Response. Response. Cal. Bias Response. Cal. Bias Percent of STACK B (2) Time (sec) PPM PPM PPM % of Soan PPM % of Soan soan Zero Gas 98 0.0 0.1 1.4 2.71% 1.3 2.50% -0.21% Upscale Gas 96 18.4 18.80 18.9 0.21% 18.4 ,0.83% -1.04%

Initial Values Final Values 3/1312008 1129 311412008 752 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift. Response Value Response. Response. Cal. Bias Response. Cal. Bias Percent of STACK 0 (4) Time (sec) PPM PPM PPM % of Soan PPM % of Span span Zero Gas 90 0.0 0 2.1 4.38% 1.0 2.08% -2.29% Upscale Gas 88 18.4 19.0 19.7 1.46% 19.4 0.83% -0.63% Initial Values Final Values 311312008 1114 3114/2008 739 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift. Response Value Response. Response. Cal. Bias Response. Cal. Bias Percent of STACKC (3) Time (sec) PPM PPM PPM % of Span PPM % of Soan span Zero Gas 103 0.0 0.0 0.0 0.00% 0.0 0.00% 0.00% Upscale Gas 108 18.4 18.8 18.2 -1.25% 18.2 -1.25% 0.00%



# 50 2 

## System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) / Span] x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) 1Span] x 100 Initial Values Final Values 3/13/2008 1043 3/14/2008 710 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift. Response Value Response. Response. Cal. Bias Response. Cal. Bias Percent of STACK A (1) Time (sec) PPM PPM PPM % of Soan PPM % of Soan soan Zero Gas 107 0.0 0.2 1.6 2.92% 1.1 1.88% -1.04% Upscale Gas 104 18.4 18.3 19.3 2.08% 18.4 0.21% -1.88% 

# BARR Engineering Company EPA METHOD 6C 50 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-range High-range Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/13-14/2008 P. Rossmiller Cylinder Serial No. CC176437 CC238857 CC68268
ANALYZER CALIBRATION DATA Certified Value 0.0 18.4 48

Note: Difference must be less than +/- 2 percent of span ····StackA·S02(1) .•...

# An~ly~erMod 

# IsK" '1OOAH Analyzer Span: 48·
.....

.... , ZeroGas .... ./ 

## Cylinder Value 

# ....if

"
... ' Mid-Rangel···>
.... ......... 

# 1M High -Range ". ..' .;. 48 .; 

# .... "



## ... Analyzer
.

Calibration.···

...

## ··ReSp?nS~ 0:2 ' •• 

# .•....
47.9 '.



# . "..

.... .... '.' 

## Absolute Difference 0.2····· '•..·.0,0·

.... 0,1 ...•• 0;06



# .. '



## .... 

## ."
.StackS-SQ2(2) "'. •••..• ••.. ...••• AnalYzer ...•.. AnalyzerModtSN100EH

# ""CYIir1der,Val~e .. Calibration P;bsolute Analyzer Span: 48
. .... .' R' '"
..... Difference

.. .'
.....;... ..... :. •.... . ....esponse ..., .' / /0.1" 0.1' ". '. 

## Zero Gas 

# .... 

# ". °
.. .'. J 

## Difference 

# as**.%ofSpa~** 

## ;.



## 0:42% •..... 0.00% ..•. 0.21% 0.13%
Difference as .%ofSpan ). "



## 0.21%

.... Low.-RanQe 

# ° 0.0
.. ' 0.00% . " ...•.••.• 18.4
. '.;. .•.... ........ 

# .18
..8 

# ..•.. High- Range ". 

## '48 ...•..' ····47:8 

# /..., ' 

# .. .'. stackG - S02(3), • ••....•. .

# .....AO~IYZer '. Analyzer Mod 

# I SN ,. 100AH .' CylinderValue '.Calibration Analyzer Span: .' 48 •• Response

, 

# .... Zero Gas 

# .. 0
.... " 0.0 . ' I..ow;; Range
......... .•... '
.. ;. " 

# o " '. '. 

## ' 

# . . ' .' ....•. Mid-Range '; 

# 1M ."
... 18.8 High. Range ..•.• 48 48.8

..



## "'ZeroGas

Low-Range Mid-Range High. Range 0.4 ,. 0;83% 0.2 • • 0.42% '., 

## Absolute DiffEirence 

# o 0;0 0.8 ." 

# .. Difference as. 

# % of Span



# . '<, 0.00% 0.00% 0.83%." 1:67%

1.25% 0.42% SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span Initial Values Final Values 

# 3/13/2008 1043 

# 3/14/2008 710 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response. Response. Cal. Bias Response. Cal. Bias STACK A (1) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 107 0.0 0.2 1.6 2.92% 1.1 1.88% Upscale Gas 104 18.4 18.3 19.3 2.08% 18.4 0.21%
Initial Values Final Values 

# 3/13/2008 1056 

# 3/14/2008 724 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response. Response. Cal. Bias Response. Cal. Bias STACK B (2) Time (sec) PPM PPM PPM % of Span PPM 

## % of Span Zero Gas 98 0.0 0.1 1.4 2.71% 1.3 2.50% Upscale Gas 96 18.4 18.80 18.9 0.21% 18.4 -0.83%
Initial Values Final Values 

# 3/13/2008 1114 

# 3/14/2008 739 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response. Response. Cal. Bias Response. Cal. Bias STACKC (3) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 103 0.0 0.0 0.0 0.00% 0.0 0.00% Upscale Gas 108 18.4 18.8 18.2 -1.25% 18.2 -1.25%
Initial Values Final Values 

# 3/13/2008 1129 

# 3/14/2008 752 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response. Response. Cal. Bias Response, Cal. Bias STACK 0 (4) Time (sec) PPM PPM PPM % 01 Span PPM % of Span Zero Gas 90 0.0 0 2.1 4.38% 1.0 2.08% Upscale Gas 88 18.4 19.0 19.7 1.46% 19.4 0.83% System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span] x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) 

# 1 Span] x 100 

# 50 2 

## Drift• Percent of

span -1.04% -1.88%

Drift. Percent of

span -0.21% -1.04%

Drift. Percent of

span 0.00% 0.00%

Drift. Percent 01

span -2.29% -0.63%

# BARR Engineering Company EPA METHOD 6C 50 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/14/08 

# AGA Cylinder Serial No. Certified Value Zero Gas CC176437 0.0 Low-range

Mid-range CC238857 18.4 Hiah-ranae CC68268 48
ANALYZER CALIBRATION DATA Note: Difference must be less than 

# +1- 2 percent of span SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span

Initial Values Final Values 3/14/2008 

# 724 3/14/2008 

# 2202 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK B (2) Time (sec) PPM PPM PPM % of Span PPM % of Soan span Zero Gas 98 0.0 0.1 1.3 2.50% 0.6 1.04% -1.46% Upscale Gas 96 18.4 18.80 18.4 -0.83% 18.5 -0.63% 0.21%

Initial Values Final Values 3/14/2008 

# 752 3/14/2008 

# 2220 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK 0 (4) Time (sec) PPM PPM PPM % of Soan PPM % of Span soan Zero Gas 90 0.0 0 1.0 2.08% 0.2 0.42% -1.67% Upscale Gas 88 18.4 19.0 19.4 0.83% 19.3 0.63% -0.21% Initial Values Final Values 3/14/2008 

# 739 3/14/2008 

# 2213 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACKC (3) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 103 0.0 0.0 0.0 0.00% -0.1 -0.21% -0.21% Upscale Gas 108 18.4 18.8 18.2 -1.25% 18.2 -1.25% 0.00%



# 50 2 

# System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span] x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) 

# 1 Span] x 100 Initial Values Final Values 3/14/2008 

# 710 3/14/2008 

# 2151 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK A (1) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 107 . 

# 0.0 0.2 1.1 1.88% 0.2 0.00% -1.88% Upscale Gas 104 18.4 18.3 18.4 0.21% 18.4 0.21% 0.00% 

# BARR Engineering Company EPA METHOD 6C 50 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-rarlfLe Hiqh-ranqe MiUal7-day Nox CEMS Furnace Scrubber Stack A-D 3/14/08 

## AGA Cylinder Serial No. CC176437 CC238857 CC68268
ANALYZER CALIBRATION DATA Certified Value 0.0 18.4 48

Note: Difference must be less than 

# +1- 2 percent of span Sta9k 

# 't-. -. S02(1)
..... ". ". 

## Analyzer Mod! SN
.. 100AH 

# ."
. . ..•.. < I Analyzer

.. ' CylindecValue. IYlIIU;>rati.on·' Absolute Differe.nce as Analyzer Span:
.48.



# . Zero 

# Gas
. . .. ;

.. ; 

## Low

# ~ Ranqe ..) Mid**~.** 

## R,;mge ';

...... High" Range
..; ..... '.

Stack 

# a**~S02(2)** 

## . "; .'. Analyzer Mod.! SN 100EH AnalyzerSpan: 48
.. 

# .' 

# ., Zero Gas
..... . 

# , LoW,:, Range' .......•.. Mid.· Range;, High - Range .'
. . ... '.' 

## Stack C - S02(3) Analyzer Moc1jSN. 100AH' Analyzer Span: '. 48 ". 

# I Respo.ns e Difference ;'. % of§pan 

# I. '.'
... ..... ...... ...... .. 

# ... 

# . .'



## .... 0.2 •... ". 0.2 • •. 0.42% .'. .• ", 0;0
. 0.00% '.' 48 47.9 • 0
.. 06
...... 0;13%



# ... ";



# .' .0
. '. ;();1 0.1



# .... 0 ....>.;. ........ ..; 

# '0.0 

# .'>' 18.4 ,,;16.6' 0.4 .'.;. ;46' '47.8 .;".0.2

'.' 

# '.' .', .' 

# I Analyzer; '. 'Absolute CylinderVa.loe. Calibration Difference Response ; 

# . . 

# .,. Difference as % of Span

0.21% 0.00% 0.63% 0.42%
'. 

## Difference as % of Span

# r-~

# __**~~z~e~ro~G~a~s~~~·.**__

# ·.<~__

# ~·;~O~~-r~···'~··'O~.O~;_·~~

# __**~O~~I** 0.00% Low - Ranqe 0 . " .• .... 0.0 % Mid-'Range .16.4· .' 18 .• 6. 

# 0.4 

# I 0.63%. High. Range 

# ;..> 46..:: 46.8 0;8 

# I
.... 1.67% " Stack D - S02(4) Analyzer Mod! SN 100AH Analyzer Span: 48

-' 

# . Zero Gas**Low~Range** 

## '.' Mid-Range " 

## High - Range • '. .'. '. .i 

# '. ;'. 

# . . .' 

## ·.··Analyzer CylinderValue
..;.' Calibration .,; Response



# .. 

# ;, . 

# '" 

# o .'
.. '. .' 0.1" Absolute Dlffere.nce 0.1 

# 0.0" 0.6 0.2 •. Difference as 

# % of Span

0.21% 0.00% .' 1.25%

0.42% SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent 01 span Initial Values Final Values 3/14/2008 

## 710 3/14/2008 

## 2151 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias STACK A (1) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 107 0.0 0.2 1.1 1.88% 0.2 0.00% Upscale Gas 104 18.4 18.3 18.4 0.21% 18.4 0.21%
Initial Values Final Values 3/14/2008 

## 724 3/14/2008 

## 2202 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias STACK B (2) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 98 0.0 0.1 1.3 2.50% 0.6 1.04% Upscale Gas 96 18.4 18.80 18.4 -0.83% 18.5 -0.63%
Initial Values Final Values 3/14/2008 

## 739 3/14/2008 

## 2213 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias STACKC (3) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 103 0.0 0.0 0.0 0.00% -0.1 -0.21% Upscale Gas 108 18.4 18.8 18.2 -1.25% 18.2 -1.25%
Initial Values Final Values 3/14/2008 

## 752 3/14/2008 

## 2220 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias STACKD (4) Time (sec) PPM PPM PPM 

# % of Span PPM % of Span Zero Gas 90 0.0 0 1.0 2.08% 0.2 0.42% Upscale Gas 88 18.4 19.0 19.4 0.83% 19.3 0.63% System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span] x 100 Drift 

# =[(Final System Cal. Response - Initial System Cal Response) 

# 1 Span] x 100 

# S02 Drift, Percent 01

span -1.88% 0.00%

Drift, Percent of

span -1.46% 0.21%

Drift, Percent of

span -0.21% 0.00%

Drift, Percent of

span -1.67% -0.21%

# BARR Engineering Company EPA METHOD 6C 50 2 

# CEMS ANALYZER CALIBRATION Project Sample Lee. Date Operators MiUal7-day Nox CEMS Furnace Scrubber Stack A-D 3/16-17/2008 

## AGA Cylinder Serial No. Certified Value Zero Gas CC176437 0.0 Low-ramie

Mid-ramie CC238857 18.4 Hiqh-ranqe CC68268 48
ANALYZER CALIBRATION DATA (analyzer span on 3/16/08) 

## Note: Difference must be less than 

# +1- 2 percent of span Stack A - S02(1) Analyzer Analyzer Mod 

# 1 SN 100AH Cylinder Value Calibration Absolute Difference as Analyzer Span: 48 Response Difference % of Span Zero Gas 0 0.0 0 0.00% Low- Range 0 0.0 0.00% Mid - Range 18.4 18.5 0.1 0.21% High - Range 48 47.9 0.1 0.21% Stack B - S02(2) Analyzer Analyzer Mod 

# 1 SN 100EH Cylinder Value Calibration Absolute Difference as Analyzer Span: 48 Response Difference % of Span Zero Gas 0 0.0 0.0 0.00% Low- Rance 0 0.0 0.00% Mid - Range 18.4 18.7 0.3 0.63% High - Range 48 48.3 0.3 0.62% Stack C - S02(3) Analyzer Analyzer Mod 

# 1 SN 100AH Cylinder Value Calibration Absolute Difference as Analyzer Span: 48 Response Difference % of Span Zero Gas 0 0.0 0 0.00% Low- Rance 0 0.0 0.00% Mid - Range 18.4 18.6 0.2 0.42% High - Range 48 48.0 0 0.00% SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span Initial Values Final Values 3/16/2008 

## 2130 3/17/2008 

## 943 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK A (1) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 107 0.0 0 0.0 0.00% 0.1 0.21% 0.21% Upscale Gas 104 18.4 18.5 18.5 0.00% 18.4 -0.21% -0.21%
Initial Values Final Values 3/16/2008 

## 2141 3/17/2008 

## 955 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK B (2) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 98 0.0 0.0 0.0 0.00% 0.3 0.63% 0.63% Upscale Gas 96 18.4 18.70 18.7 0.00% 18.5 -0.42% -0.42%
Initial Values Final Values 3/16/2008 

## 2151 3/17/2008 

## 1009 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACKC (3) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 103 0.0 0.0 -0.5 -1.04% -0.2 -0.48% 0.56% Upscale Gas 108 18.4 18.6 18.6 0.00% 18.6 0.00% 0.00%
Initial Values Final Values 3/16/2008 

## 2153 3/17/2008 

## 1017 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK D(4) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 90 0.0 0 0.0 0.00% 0.4 0.83% 0.83% Upscale Gas 88 18.4 18.7 18.7 0.00% 18.8 0.21% 0.21% Stack D - S02(4) Analyzer Analyzer Mod 

# 1 SN 100AH Cylinder Value Calibration Absolute Difference as Analyzer Span: 48 Response Difference % of Span Zero Gas 0 -0.1 0.1 0.21% Low- Rance 0 0.0 0.00% Mid - Range 18.4 18.7 0.3 0.63% High - Range 48 48.1 0.1 0.21% System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span] x 100 Drift 

# =[(Final System Cal. Response -Initial System Cal Response) 

# 1 Span] x 100 

# S02 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-range High-range MiUal7-day Nox CEMS Furnace Scrubber Stack A-D 3/16-17/2008 

# AGA Cylinder Serial No. CC176437 CC238857 CC68268 Certified Value 0.0 18.4 48
ANALYZER CALIBRATION DATA (analyzer span on 3/16/08) 

# Note: Difference must be less than 

# +1- 2 percent of span Stack A - S02(1) Analyzer Analyzer Mod 

# 1 SN 100AH Cylinder Value Calibration Analyzer Span: 48 Response Zero Gas 0 0.0 Low- Range 0 Mid - Range 18.4 18.5 High - Range 48 47.9 Stack B - S02(2) Analyzer Analyzer Mod 

# 1 SN 100EH Cylinder Value Calibration Analyzer Span: 48 Response Zero Gas 0 0.0 Low- Ranqe 0 Mid - Range 18.4 18.7 High - Range 48 48.3 Stack C - S02(3) Analyzer Analyzer Mod 

# 1 SN 100AH Cylinder Value Calibration Analyzer Span: 48 Response Zero Gas 0 0.0 Low- Range 0 Mid - Range 18.4 18.6 High - Range 48 48.0 Stack D - S02(4) Analyzer Analyzer Mod 

# 1 SN 100AH Cylinder Value Calibration Analyzer Span: 48 Response Zero Gas 0 -0.1 Low- Range 0 Mid - Range 18.4 18.7 High - Range 48 48.1 Absolute Difference 0 0.0 0.1 0.1
Absolute Difference 0.0 0.0 0.3 0.3
Absolute Difference 0 0.0 0.2 0
Absolute Difference 0.1 0.0 0.3 0.1 

# EPA METHOD 6C S02 CEMS ANALYZER CALIBRATION

Difference as

% of Span

0.00% 0.00% 0.21% 0.21%
Difference as % of Span

0.00% 0.00% 0.63% 0.62%
Difference as % of Span

0.00% 0.00% 0.42% 0.00%
Difference as % of Span

0.21% 0.00% 0.63% 0.21% SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span Initial Values Final Values 3/16/2008 

# 2130 3/17/2008 

# 943 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias STACK A (1) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 107 0.0 0 0.0 0.00% 0.1 0.21% Upscale Gas 104 18.4 18.5 18.5 0.00% 18.4 -0.21%
Initial Values Final Values 3/16/2008 

# 2141 3/17/2008 

# 955 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias STACK B (2) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 98 0.0 0.0 0.0 0.00% 0.3 0.63% Upscale Gas 96 18.4 18.70 18.7 0.00% 18.5 -0.42%
Initial Values Final Values 3/16/2008 

# 2151 3/17/2008 

# 1009 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias STACKC (3) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 103 0.0 0.0 -0.5 -1.04% -0.2 -0.48% Upscale Gas 108 18.4 18.6 18.6 0.00% 18.6 0.00%
Initial Values Final Values 3/16/2008 

# 2153 3/17/2008 

# 1017 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias STACK D(4) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 90 0.0 0 0.0 0.00% 0.4 0.83% Upscale Gas 88 18.4 18.7 18.7 0.00% 18.8 0.21% System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span] x 100 Drift 

# =[(Final System Cal. Response -Initial System Cal Response) 

# 1 Span] x 100 

# S02 Drift, Percent of

span 0.21% -0.21%

Drift, Percent of

span 0.63% -0.42%

Drift, Percent of

span 0.56% 0.00%

Drift, Percent of

span 0.83% 0.21%

# BARR Engineering Company EPA METHOD 6C S02 CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/17-18/2008 AGA Cylinder Serial No. Certified Value Zero Gas CC176437 0.0 Low-range

Mid-range CC238857 18.4 High-range CC68268 48
ANALYZER CALIBRATION DATA Note: Difference must be less than 

# +/- 2 percent of span SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed +/- 

# 5 percent of span. Drift cannot exceed +/- 

# 7.5 percent of span

Initial Values Final Values 3/17/2008 1009 3/18/2008 855 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACKC (3) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 103 0.0 0.0 -0.2 -0.48% 0.4 0.83% 1.31% Upscale Gas 108 18.4 18.6 18.6 0.00% 18.8 0.42% 0.42%
Initial Values Final Values 3/17/2008 1017 3/18/2008 914 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK D(4) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 90 0.0 0 0.4 0.83% 0.7 1.46% 0.63% Upscale Gas 88 18.4 18.7 18.8 0.21% 18.9 0.42% 0.21% Initial Values Final Values 3/17/2008 955 3/18/2008 843 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK B (2) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 98 0.0 0.0 0.3 0.63% 0.8 1.67% 1.04% Upscale Gas 96 18.4 18.70 18.5 -0.42% 18.8 0.21% 0.63%



# S02 System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) / Span] x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) / Span] x 100 Initial Values Final Values 3/17/2008 943 3/18/2008 831 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK A (1) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 107 0.0 0 0.1 0.21% 0.7 1.46% 1.25% Upscale Gas 104 18.4 18.5 18.4 -0.21% 18.2 -0.63% -0.42% 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-range High-range Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/17-18/2008 

# AGA Cylinder Serial No. CC176437 CC238857 CC68268
ANALYZER CALIBRATION DATA Certified Value 0.0 18.4 48

Note: Difference must be less than 

# +1- 2 percent of span "S!'lckjl.- Sq2(1) ..•. 

# .... . 

# ... Ar)alyzerl\l!od/sN 100AI{ Cylinder Vctlue Analyzer .'. AlialyzetSpan; 48 Calibration Response



# .... . 

## ;'" 

# . •...... Zero Gas .' 

# .... 

# .. . 0 " 

# ..•.. 0.0



# ..
. " 

# Low;·RanQe 

# . o ' . .' 

# ..

....... 

# ,. Mid. Range 

# .. ' 

# ...... 

# 1M.' 18.5
... '

, 

# HiglJ·Range • 

# . 48 47.9 

# .'.



# .... ..... '.**.Sta~KB.-** 

# S02(2)
. 

# '. j1.naIYZElfMBdISN 100EH Analyzer CYI.inderValue Calibration**J1.nal~zerSpan:** 

# 48


# ....**Respons~** 

# I·
.. · . · .... ZeroGas . 

# ,. .' 

### '. 

# 0 .··.0.0 

# .•... 

# . ..; 

# Absolute.····· Difference:



# . ;.' 

# .'. 0 

# '. 0:0 

# ..' 

# ,. 0:1 0.1. : 

# .'. Absqlute' Differencfil

,. / 

# . 

# 0:0 

# EPA METHOD 6C S02 CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span


# .. ". 

# Initial Values Final Values Difference as 3/17/2008 

# 943 3/18/2008 

# 831

%ofSpan Cylinder Analyzer Cal System Cal System Cal System Cal System Cal <,' • 

# Response Value Response, Response, Cal. Bias Response, Cal. Bias**"'O~OO%'** 

# '. STACK A (1) Time (sec) PPM PPM PPM % of Span PPM % of Span "'0:00% Zero Gas 107 0.0 0 0.1 0.21% 0.7 1.46% .; 

# 0,21"10 

# '. Upscale Gas 104 18.4 18.5 18.4 -0.21% 18.2 -0.63% ····.·0.21% i···· . ". .' 

# Initial Values Final Values Difffilren,ce as 3/17/2008 

# 955 3/18/2008 

# 843 ;%o{Span Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response. Response, Cal. Bias Response, Cal. Bias ·····0.00% STACK B (2) Time (sec) PPM PPM PPM % of Span PPM % of Span

..**Low~Range·,** 

# \ o '. 

# ',"

........ 0.0 .... ··.o.CO%
. Zero Gas 98 0.0 0.0 0.3 0.63% 0.8 1.67% 

# ..•..•.........**Mid':Rang~** 

# . 18.4
.... 18.7 ·.i 0.3;
.. ··.• ···0.63%

.... High ; Range 

# . 48
... , 

# 48.3 

# . 0:3
. • ():62% '.' 

### '. '" " 

# . StackC-S02(3) , •• 

# .... 

# ....... . 

# ..... Analyzer Absolute

# Anaiy~er.Mod 

# 1SN.·· 100AH Cylinder Value Calibration Difference as Analyzer Span: 48 i 

# ReSPOnse Difference

# I'''o~o q(Span



# . .' 

# .

.....

# ,. Zero Gas ". 

# 0 0.0 o. 

# .. 0.00% Low" Ranqe 0 

# . . 0.0 

# ....... 0.00% '
..

# Mid~.Range , 

# 18.4 '
... 18.6 0:2 ". 

# ..... 0:42%. ",

High-Range '. 

# .' 

# 48 48.0 .0 0.00% '. 

# '.,

.. 

# " ". 

# .. '.' 

# • .... Stack D-S02(4) : 

# .' '.; Analyzer Mod} SN 100AH 

# . Analyzer Absolute Difference as Cylinder Value. Calibration Analyzer Span: 48 Response Differen.ce % of Span



# .... ... ; ...... 

# .. . ' 

# I, .... Zero.Gas 

# . 0 ' 

# .**~0.1** 

# 0.1 0.21% .•··"··low

# ~ Range '. 

## .' 

# . ' 0 

# . 0.0. '.0.00% Mid. Range 18.4 18;7**O:~··** 

# 0.63% High.-Range 48 48.1 0:1 0.21% Upscale Gas 96 18.4 18.70 18.5 -0.42% 18.8 0.21%
Initial Values Final Values 3/17/2008 

# 1009 3/18/2008 

# 855 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias STACKC (3) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 103 0.0 0.0 -0.2 -0.48% 0.4 0.83% Upscale Gas 108 18.4 18.6 18.6 0.00% 18.8 0.42%
Initial Values Final Values 3/17/2008 

# 1017 3/18/2008 

# 914 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response
. Response, Cal. Bias Response. Cal. Bias STACK D(4) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 90 0.0 

# a 0.4 0.83% 0.7 1.46% Upscale Gas 88 18.4 18.7 18.8 0.21% 18.9 0.42% System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) I Span] x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) I Span] x 100 

# S02 Drift, Percent of

span 1.25% -0.42%

Drift, Percent of

span 1.04% 0.63%

Drift, Percent of

span 1.31% 0.42%

Drift. Percent of

span 0.63% 0.21%

# BARR Engineering Company EPA METHOD 6C 50 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/18-19/2008 AGA Cvlinder Serial No. Certified Value Zero Gas CC176437 0.0 

# Low-rance

Mid-ranqe CC238857 18.4 Hiqh-ranqe CC68268 48

Initial Values Final Values 3/18/2008 855 3/19/2008 740 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACKC (3) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 103 0.0 0.0 0.4 0.83% 0.2 0.42% -0.42% Upscale Gas 108 18.4 18.6 18.8 0.42% 19.0 0.83% 0.42% Initial Values Final Values 3/18/2008 831 3/19/2008 709 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK A (1) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 107 0.0 0 0.7 1.46°/" 0.7 1.46% 0.00% Upscale Gas 104 18.4 18.5 18.2 -0.63% 18.5 0.00% 0.63%
Initial Values Final Values 3/18/2008 843 3/19/2008 725 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACKB (2) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 98 0.0 0.0 0.8 1.67% 0.7 1.46% -0.21% Upscale Gas 96 18.4 18.70 18.8 0.21% 18.6 -0.21% -0.42%



# 50 2 

## SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed 

## +/- 5 percent of span. Drift cannot exceed 

## +/- 7.5 percent of span

System Calibralion Bias - [(System Cal. Response - Analyzer Cal. Response) / Span] x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) / Span] x 100 Initial Values Final Values 3/18/2008 914 3/19/2008 758 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACKD (4) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 90 0.0 0 0.7 1.46% 1.0 2.08% 0.63% Upscale Gas 88 18.4 18.7 18.9 0.42% 18.8 0.21% -0.21%



# - ANALYZER CALIBRATION DATA Note: Difference must be less than 

# +/- 2 percent of span .:l/"lt:) 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-range High-range Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/18-19/2.0.08 AGA Cylinder Serial No. CC176437 CC238857 CC68268 ANALYZER CALIBRATION DATA Certified Value .0
..0 18.4 48

Note: Difference must be less than +1- 

# 2 percent of span .:)/"It) 

### (g) [I UU

# St~Ck'A:&02(1) 

# . ! 

# .... 

# . j ..•. ' .! .....•..•.



# Analyzer AnalyierlYlod/SN 1GGAH 1····••

# CYlinderV~lue. Calior"tion Absolute •• Analyzer Span:· 

# .;. 48 Response .'. p.ifference ••.•.



# . ". '!' .• 

# .... i'.; j" ..•. f •• 

# s 

# I. • .....
•• 

# < Zero·Gas 

# ....... 

# ... ' .

# .. .0 

# . ". 

# . .0
. .0 

# .. '.'
..0 

# .' ! .• 

# LOW.Range: .... .! 

## foe) 

# .0 . '


# .. . ' 

# .....• 

# .0.0 •...••.' . Mid ".Range.; fi'" 

# ....... 18.4 .'.! 

# 18.5 .0.1 HillIl- Range , 

# 48 47.9 

# .f .0.1
j •••• 

# > ... . 

# ..... ' 

## .. '



# . Stack B.- S02(2)../ .' 'j' 

# Cylin0!'lrValue Analyzer 

# I·' '. Absolu'\e AnalYzTr Mod I.SN·· ···.·1 GGEH .'
.... Calibration Analyzer**Spa~:·.48** 

# ... "; j 

# Response. Difference <,</,«,; 

# '. .'.


# ........ 

# , 

# ............

. Zero Gas 

# ..'
....

# "

........ ! 

# .0 

# ......

# , ... 

# .... .0
..0 .' 

# .0• .0 ...•

.. ' 

# LOw-Range :


# . .' ..•. :;' .0 .'. 

# .'
, '. ! 

# .0
. .0 ! ,.f
......

## Mid.~Rafige 

# . 18.4 .' 

# 18.7 ,



# . .0.3" .j' 

# .'. 

# High .,Range '
.. ! .• 

# . 48 48.3 1 

# .0.3 .i·



## .. ' 

# .... j j' 

# .'. ..... . /


# . <Stack C - S02.(3)
..... . 

# ... 

# Analyzer Mod 

# I SN 1GGAH Analyzer I'·· Absolute Analyzer Spa!): .:", 

# .,. 

# 48·' Cylinder Value Calibration. Difference Response

.. j



## .... 

# .... 

# Zero Gas 

# .' .;, 

# I;·.·· .f 

# G' '. 

# .0
..0 .0 '. 

# : Low" Range 

# , .0 

# , .0
..0 .... 

# •..••. Mid -Range .' 

# ..

# ', 

# .18.4 18.6 .0.2



# .. High' Range 

# . .. . 

# .' 48 : 

# 48
..0 

# .0 !. 

### ". 

### ! 

# .' 

# . Stack D - S02(4) 

# . f

# Analy~e~ Mod/SN 1GGAH Analyzer Absolute ,Cylinder Value Calibration Analyzer 9pan: . '·.48: 

# I
.. ··· .' ! ' •. '. 

# Response Difference • ! 

# .. '> ., .. , 

# Zero Gas 1 

# .0 -.0;1 ". 

# .0.1 ".



# .**LOW~'Ranile** f. 

### ii: ' . 

# G·
... .' 

# .0
..0 Mid -Range ..... 

# ' 18.4 -'" 

### : 

# 18.7 .' 

# .0.3 High -. Range '.' 

# :.' 48 ;, 

# 48.1 .0.1 I



# . EPA METHOD 6C 50 2 

# CEMS ANALYZER CALIBRATION

# Ojffer~nceas.

%pfSpan
.:. i !
.. 

## j! •



# .0,.00"10 .0•

.0.0% .0.21% 0'.21%

.... '" 

# , ..... 

# ,

.. '" 

# ...**Oifference~s** 

# . % of Span
of 

### .' 

# ... ' 

# 0,0.0% .0;.0.0% ',., .0.63% .0:62%

'" f 

### ; 

# Difference as

% of Span



# ••

.. ' 

# .0
..0.0%
..,!'. 

# .:. .0:.0.0% 

# .', .0.42.% ..' 

# .0:.0.0%

.... ' 

# . 

# DifferenCe as ·.%ofSpan : ! ••.. 

### 'j
. 

# .0.21% .. 

# .0:.0.0% .0.63%

.... .0.21% SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed +1- 

# 5 percent of span. Drift cannot exceed +1- 

# 7.5 percent of span Initial Values Final Values 3/18/2.0.08 831 3/19/2.0.08 7.09 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias STACK A (1) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 1.07 .0
..0 .0 .0.7 1.46% .0.7 1.46% Upscale Gas 1.04 18.4 18.5 18.2 -.0.63% 18.5 .0
..0.0%
Initial Values Final Values 3/18/2.0.08 843 3/19/2.0.08 725 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response. Response, Cal. Bias Response, Cal. Bias STACKB (2) Time (sec) PPM PPM PPM % of Span PPM % 

# of Span Zero Gas 98 .0
..0 .0
..0 .0.8 1.67% .0.7 1.46% Upscale Gas 96 18.4 18.7.0 18.8 .0.21% 18.6 -.0.21%
Initial Values Final Values 3/18/2.0.08 855 3/19/2.0.08 74.0 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response. Cal. Bias STACKC (3) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 1.03 .0
..0 .0
..0 .0.4 .0.83% .0.2 .0.42% Upscale Gas 1.08 18.4 18.6 18.8 .0.42% 19
..0 .0.83%
Initial Values Final Values 3/18/2.0.08 914 3/19/2.0.08 758 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response. Response, Cal. Bias Response, Cal. Bias STACKD (4) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 9.0 .0
..0 .0 .0.7 1.46% 1 ..0 2 ..08% Upscale Gas 88 18.4 18.7 18.9 .0.42% 18.8 .0.21%



# - System Calibralion Bias - [(System Cal. Response - Analyzer Cal. Response) I 

# Span] x 1.0.0 Drift 

# =[(Final System Cal. Response - Initial System Cal Response) I 

# Span] x 100 

# S02 Drift, Percent of

span .0
..0.0% .0.63%

Drift, Percent of

span -.0.21% -.0.42%

Drift, Percent of

span -.0.42% .0.42%

Drift. Percent of

span .0.63% -.0.21%

# BARR Engineering Company EPA METHOD 6C 50 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/19-20/2008 AGA Cylinder Serial No. Certified Value Zero Gas CC176437 0.0 Low-rance

Mid-ranqe CC238857 18.4 Hiqh-ranqe CC68268 48

Initial Values Final Values 3/19/2008 740 3/20/2008 743 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACKC (3) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 103 0.0 0.0 0.2 0.42% 0.4 0.83% 0.42% Upscale Gas 108 18.4 18.6 19.0 0.83% 19.6 2.08% 1.25%
Initial Values Final Values 3/19/2008 758 3/20/2008 756 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACKD (4) Time (sec) PPM PPM PPM % of Soan PPM % of Soan soan Zero Gas 90 0.0 0 1.0 2.08% 0.9 1.88% -0.21% Upscale Gas 88 18.4 18.7 18.8 0.21% 18.8 0.21% 0.00% Initial Values Final Values 3/19/2008 725 3/20/2008 726 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK B (2) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 98 0.0 0.0 0.7 1.46% 0.8 1.67% 0.21% Upscale Gas 96 18.4 18.70 18.6 -0.21% 18.9 0.42% 0.62%



# S02 SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed 

# +/- 5 percent of span. Drift cannot exceed 

# +/- 7.5 percent of span

System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) / Span] x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) / Span] x 100 Initial Values Final Values 3/19/2008 709 3/20/2008 713 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK A (1) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 107 0.0 0 0.7 1.46% 0.9 1.88% 0.42% Upscale Gas 104 18.4 18.5 18.5 0.00% 18.2 -0.63% -0.63% ANALYZER CALIBRATION DATA Note: Difference must be less than 

# +/- 2 percent of span .:lrlb 

## (fJJ L'lUU 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-range High-range Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 

# 3/19-20/2008 AGA Cylinder Serial No. CC176437 CC238857 CC68268
ANALYZER CALIBRATION DATA Certified Value 0.0 18.4 48

Note: Difference must be less than 

# +1- 2 percent of span .:)rlb (f!J L'lUU 

# Stac.kA - S02(1) 

# ...• AnalY2er Analyzer ModlSN 100AH 

# . i ..· ..···· '. " AnalY2er
.. Span: 

# < 

# 48 Cylinpervalue

# Calibratio~ . ' Response


# .. . 

### ; 

# . ';'" 

# .'. ! "
......'. ;'
. 

# Zero.Gas 

# . '" 

# .0 0.0 ;. 

# Low- Rangei<
.......... , ..... 0 

# ....•.
.; 

# Mid**~Range** 

# ....... 

# 18.4 • 18.5 " 

# High • Range ;." 

# 48' 

# , 47:9 

# .' .. .'. 

# '. '; Stack**~** 

# ·S02(2) AnalY2er '. AnalyzerModlSN fOOEt-! '.' 

# Cylinder Value '. '.' Calibration
.. ' AnCjlyzer Span: 

# > ··48
.... ". 

# Response 

# .....•.•... .'.;." 

# '

# .. ). 

# Zero Gas ." • 

# 0 

# .... 0.0 .' 

# Low-+RanQe .,. 

# · ...•. ···0···· ."



# . •. ·.Mid,; Range


# .... 

# , 18.4 18.7 .' 

# High -Range 

# . 

# ... 48 .' 

# 48:3



# . ' 

# ..' 

# : 

# . 

# . '" SlackC- 502(3) '
..' 

# .... Analyzer Analyzer Mod 

# 1 SN '100AH

. qYllndervalue' ! 

# Calibration Analyzer Span: 48 ..•. Response '. 

# . Zero Gas 

# · . 0.··· > 0.0 

# . '. 

# Low-Range 

# ..•........ 

# .... '. 

# o .,.; ' 

# . .... .' 

# Mid -.Range
. .' 

# .'. 18.4. 1.8:6
.. High':' Range ;

## .... 

# '. 48 ." 

# 48:0
.AnalY2er Caiibration Response

-0.1 18.7 48.1 ..... 

# Absolute Difference



# . '.' 

# ", I 

# 0 0:0 0.1 ". 

# 0.1



# .. ' 

# .. '. 

# Absolute Difference

" 

# . 0.0 0.0 ! 

# 0.3 0.3
Absolute • Difference 

# 6 0.0 0.2 0
Absolute Difference 0.1 0.0 0.3 0.1 

# EPA METHOD 6C 50 2 

# CEMS ANALYZER CALIBRATION

Dlffe(enceas 

# "10. of Span '. ". 

# 0.00% 0.000/ • 0.21% 0.21%' '. 

# Difference as



# % of Span



# .... 0.00%'
. 0.00% 0,63% 0.62%



# . Differenc::e as % of Span 

# , 0.00% ' ·0.00%

0.42% ..•. 0.00%
Difference as

%ofSpan

0.21% 0.00% 0.63% 0.21% SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span Initial Values Final Values 

# 3/19/2008 709 

# 3/20/2008 713 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias STACK A (1) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 107 0.0 0 0.7 1.46% 0.9 1.88% Upscale Gas 104 18.4 18.5 18.5 0.00% 18.2 -0.63%
Initial Values Final Values 

# 3/19/2008 725 

# 3/20/2008 726 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response. Response, Cal. Bias Response, Cal. Bias STACK B (2) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 98 0.0 0.0 0.7 1.46% 0.8 1.67% Upscale Gas 96 18.4 18.70 18.6 -0.21% 18.9 0.42%
Initial Values Final Values 

# 3/19/2008 740 

# 3/20/2008 743 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias STACKC (3) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 103 0.0 0.0 0.2 0.42% 0.4 0.83% Upscale Gas 108 18.4 18.6 19.0 0.83% 19.6 2.08%
Initial Values Final Values 

# 3/19/2008 758 

# 3/20/2008 756 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response. Response, Cal. Bias Response, Cal. Bias STACKD (4) Time (sec) PPM PPM PPM % of Span PPM % of Soan Zero Gas 90 0.0 0 1.0 2.08% 0.9 1.88% Upscale Gas 88 18.4 18.7 18.8 0.21% 18.8 0.21% System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span] x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) 

# 1 Span] x 100 

# S02 Drift. Percent of

span 0.42% -0.63%

Drift, Percent of

span 0.21% 0.62%

Drift, Percent of

span 0.42% 1.25%

Drift, Percent of

span -0.21% 0.00%

# BARR Engineering Company EPA METHOD 6C 502 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/20-21/2008 AGA Cvlinder Serial No. Certified Value Zero Gas CC176437 0.0 

# Low-rance

Mid-ranoe CC238857 18.4 

# Hiqh-rance CC68268 48

Initial Values Final Values 3/20/2008 726 3/21/2008 843 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACKC (3) Time (sec) PPM PPM PPM % of Soan PPM % of Soan soan Zero Gas 103 0.0 0.0 0.8 1.67% 1.6 3.33% 1.67% Upscale Gas 108 18.4 18.60 18.9 0.62% 19.3 1.46% 0.83% Initial Values Final Values Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACKB (2) Time (sec) PPM PPM PPM % of Soan PPM % of Soan soan Zero Gas Upscale Gas Initial Values Final Values 3/20/2008 713 3/21/2008 810 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK A (1) Time (sec) PPM PPM PPM % of Soan PPM % of Soan soan Zero Gas 107 0.0 0 0.9 1.88% 0.7 1.46% -0.42% Upscale Gas 104 18.4 18.5 18.2 -0.63% 18.7 0.42% 1.04%



# S02 SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed +/- 

# 5 percent of span. Drift cannot exceed +/- 

# 7.5 percent of span

System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) / Span] x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) / Span] x 100 Initial Values Final Values 3/20/2008 756 3/21/2008 851 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response. Response. Cal. Bias Response, Cal. Bias Percent of STACK 0(4) Time (sec) PPM PPM PPM % of Soan PPM % of Span soan Zero Gas 90 0.0 0 0.9 1.88% 0.6 1.25% -0.63% Upscale Gas 88 18.4 18.7 18.8 0.21% 18.8 0.21% 0.00%



# - ANALYZER CALIBRATION DATA Note: Difference must be less than 

# +/- 2 percent of span 

# "no!$ L'IUU 

# BARR Engineering Company EPA METHOD 6C 502 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators

Zero Gas Low-ranqe

Mid-ranqe High-ranqe Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/20-21/2008 AGA Cylinder Serial No. CC176437 CC238857 CC68268
ANALYZER CALIBRATION DATA Certified Value 0.0 18.4 48

Note: Difference must be less than 

# +/- 2 percent of span 

# "no!$ L',UU 

## StackA-S02(1)
..... •••.•• ··.ArlaIYzer
. ".
.......... .., .. AnalyzerM9dJ SN1OOAH

# ~.. . Cylinder 

# Value Calibration Absolutt;l Difference as Analyzer Span: "... .48 . '
.. ' Response" Difference 'Yo of Sp;;\n


# . ..,... .. ·1...
.. . ... • ... '

.. • •.. Zero Gas' 

# I'.... ..0 

# f
.. '
... • 0.0
. .. 0.···· 0:00%
... '

. Low-Range .•...• 10 

# 1«... 0.0
.... 0.00%

High - Range._ ....••. 48 '47.9. '" 0:1 .':.' 

# .... ..... . .... 

# , Stack 

# B - S02(2)**Anl(lly~er ~9d**  

# I SN 100EH AnalyzerSpao: 48 

# . ":.;,. ..' I. '. '. ..•..•. '. 

## AnalY2: er Ab 

# I 

# t 

# I.' Cylinder

# Y~lue I.:.·.·

# Call9ra~lo!1 '.'

# Diff~~tl~~ .• '"
.......... RespOnst;l Zero Gas 0", '.' 0.0:·0;0

... ' Low" Range
. '. 

# o ..... 1 ...• .... 

## 0.0 

# 1M '.' '.' ..•.....•.Ht7........•..' 0.3 '.' High - Range 

# . ". 

## 48
.... 48:3. :.'. 0.3



# .. . ... Staqk C -. S02(3) Analyzer Mod / SN" ··1ooAH Analyzer Span: 48 

# .'. Zerd Gas 

# ...... .'. Low - Ranqe ."

Mid- Range ..•.••.. High - Range

StackD- S02(4)**Af'laly~er** 

## ModI SN. .:.-..,....:..10::.:0::.A::,.H!.--j AnalyzerSpan: 48 •

.. 

# I Zero Gas·' ". Low - Range • '.

.;.'
... Mid - Range '" 

## High - Range .' 

## . . '.' .' ." ; Analyzer '"

# CYh~deryalue Calibr\ltiol1..

# ~bsolute "ResponsE!' '. Difference

'- :0.0··.····· '.. '.' ······1·· 

# 18.4 48 •.. 

# '

.. '; 

# .....

. " 

## .•.....•....... Cylinder Value.

'

# .. '



# .···0 

# ......

. " 0 

# '. 1.8.4 

# ..

.... 48' 

# .. I 

# .i' 18.6
..' 48.0 .• '



# . .' Analyzer
..: ...• .Calibration Response 

# '.' -0.1



# .. •• 18.7 • 48.1 '.' 

### I 

# ..... 

# o 0:0 0.2 

# o
Absolute Difference



# . 0.1

.0.0 0.3 0.1 

# .. ;0.21% 0.21% :. 

## :' 

# ". Difference as % of Span 

# ·····ll.OO% 0.00% .' '0.63% .'.

0.62%·',
Difference as % of Span

0.00%
. 0.00% • 0.42%

0.00%
Difference as %.ofSpan •.



# , 0.21% '. ·0.00% ...•.. 0.63%

.'. 0.21%' SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span Initial Values Final Values 

# 3/20/2008 713 

# 3/21/2008 810 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias STACK A (1) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 107 0.0 0 0.9 1.88% 0.7 1.46% Upscale Gas 104 18.4 18.5 18.2 -0.63% 18.7 0.42%
Initial Values Final Values Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias STACKB (2) 

## Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas Upscale Gas
Initial Values Final Values 

# 3/20/2008 726 

# 3/21/2008 843 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response. Response, Cal. Bias Response, Cal. Bias STACKC (3) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 103 0.0 0.0 0.8 1.67% 1.6 3.33% Upscale Gas 108 18.4 18.60 18.9 0.62% 19.3 1.46%
Initial Values Final Values 

# 3/20/2008 756 

# 3/21/2008 851 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response. Response. Cal. Bias Response, Cal. Bias STACK 

# 0(4) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 90 0.0 0 0.9 1.88% 0.6 1.25% Upscale Gas 88 18.4 18.7 18.8 0.21% 18.8 0.21%



# - System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span] x 100 Drift 

# = [(Final System Cal. Response -Initial System Cal Response) 

# 1 Span] x 100 

# S02 Drift, Percent of

span -0.42% 1.04%

Drift, Percent of

span

Drift, Percent of

span 1.67% 0.83%

Drift, Percent of

span -0.63% 0.00%

# BARR Engineering Company EPA METHOD 6C 50 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mittal 7-day Nox CEMS Furnace Scrubber Stack A-D 3121-2212008 AGA Cylinder Serial No. Certified Value Zero Gas CC176437 0.0 

# Low-rance

Mid-ranqe CC238857 18.4 Hiqh-ranqe CC68268 48

Initial Values Final Values Cylinder Analyzer Cal Systern Cal System Cal System Cal Systern Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK B (2) Time (sec) PPM PPM PPM % of Span PPM % of Soan span Zero Gas Upscale Gas
Initial Values Final Values 312112008 843 312212008 746 Cylinder Analyzer Cal Systern Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK C (3) Time (sec) PPM PPM PPM % of Soan PPM % of Span soan Zero Gas 103 0.0 0.0 1.6 3.33% 1.6 3.33% 0.00% Upscale Gas 108 18.4 18.60 19.3 1.46% 19.7 2.29% 0.83% Initial Values Final Values 312112008 810 312212008 726 Cylinder Analyzer Cal System Cal System Cal Systern Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK A (1) Tirne (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 107 0.0 0 0.7 1.46% 0.3 0.63% -0.83% Upscale Gas 104 18.4 18.5 18.7 0.42% 18.1 -0.83%**~1.25%**



# S02 SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed +1-5 percent of span. Drift cannot exceed +1-7.5 percent of span

System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 1Span] x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) 1Span] x 100 Initial Values Final Values 312112008 851 312212008 756 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK D (4) Time (sec) PPM PPM PPM % of Soan PPM % of Soan soan Zero Gas 90 0.0 0 0.6 1.25% 1.0 2.08% 0.83% Upscale Gas 88 18.4 18.7 18.8 0.21% 18.7 0.00% -0.21%



# - ANALYZER CALIBRATION DATA Note: Difference must be less than +1-2 percent of span ,j/'lt,@L'IUU 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-range High-range Mittal 7-day Nox CEMS Furnace Scrubber Stack A-D 3121-2212008 AGA Cylinder Serial No. CC176437 CC238857 CC68268
ANALYZER CALIBRATION DATA Certified Value 0.0 18.4 48

Note: Difference must be less than +1- 2 percent of span .l/'lt,@L·IUU



# .... Stack**~.** 

## S9,2(1) 

# ... " 

### . 

## 'XnaJyzer Analyzer MqdJ**S~** 

## 100AH .'
.

# Cylinde~Value AnalY2er Span: Calibration 48 R.esponse


# .........

....... Zeto Gas .' '.' 

# ....• 

# (f·.·
.. '·";"0.0'
" 

# .......**Low~** 

## Range 

# ",oC .' ?: 

# ' 

# .

.. Mid· Range 

# .. ' 

## ' .• 1.8.4 .... ·'18.5 

# < .' 

## High· Range 

# ........... . ; 

# .; 48 

# .. .47.9



# .. 

# .. '.'

-



## ··StackB· S02(2) 

# .. Analyzer Mod 

# I 5N 100EH CylinderValue

# IAnalyze~ Analyzer Span: 

# < 48 Calibratio(l
..


# , ••••**Respon~e** •• 

# '. " .Zero Gas 

# .... 0 . 

## 0.0 

# , 

# ··.·.··t.:ow· RanQe 

# , 0 

# .. ....

# ' ..•. 

# : . Absolute Dlfferenc;e



# .



# .. , .' o· 0;0 

# . .0.1 

# '.' .'0:1"

.' .' 

# '.'**·.Ab~olute** 

## Difference



# .;. 0.0' ' . :

# .. 0.0 

# EPA METHOD 6C 50 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed +1- 5 percent of span. Drift cannot exceed +1- 7.5 percent of span I: Initial Values Final Values

Difference as 312112008 810 312212008 726

%ofSp<\n Cylinder Analyzer Cal System Cal System Cal Systern Cal System Cal



# . ,> 

## Response Value Response, Response, Cal. Bias Response, Cal. Bias 0,00% STACK A (1) Tirne (sec) PPM PPM PPM % of Span PPM % of Span 

# I
.. 0.00% Zero Gas 107 0.0 0 0.7 1.46% 0.3 0.63% 0.21% Upscale Gas 104 18.4 18.5 18.7 0.42% 18.1 -0.83% 0.21% •

.. 

## Initial Values Final Values Difference. as % ofSpan Cylinder Analyzer Cal Systern Cal System Cal System Cal Systern Cal '. 

## Response Value Response, Response, Cal. Bias Response, Cal. Bias 0.00% STACK B (2) Time (sec) PPM PPM PPM % of Span PPM % of Span 

# .' 0.00% Zero Gas Mid· Range "'18,4 "18.7

. 

## " 

# ... 0:3 0.63% Upscale Gas High· Range' ". 

# .... 48 48:3 ·.·0;3
... · 0.62%



# . ' 

# .',
.... 

# .' ", " 

# ... ' 

## Stack C • SO:1(3)



# . '" 

# I 

# ... .. AnalyzerMod ISN 100AH ••**Al1al~er** 

## Absolute Difference as Analyzer Span: .48 Cylinder Vallie '" Calibra.tion Difference .' %. of Span Resp.onse. , '. .'

# .......... ",


# ..... .' 

## Zero Gas 

# . 0 ". 

## '. ·'0.0, " 

## 0 0.00%

. '. LoW" Range .' 

## 0 

# • I I•. 0.0 ." 0.00% Mid.· Range 

# 18.4
.......... 1.8.:6
..'
.. , " 

## 0.2 0,42% High· Range 48 '. 

## 48:0 " .'. , 

## 0 0.00%



# . . " 

# ....

.. 

## .•...... ..•. 

### ." 

## Stack 0 • S02(4) 

# . ....... •....... Analyzer Modi SN 100AH .' I CyljnderValue Analyzl'lr, • Absolute Difference as Analyzer Span: Calibration pifference % of Span 48 Response I
...... ' 

# . 

# " Zero Gas 0 

# . " 

## ,.-0.1 

# .....•

.. 0.1 0:21%

.. Low, Range 

# . 0 " 

# .... 

# .' 

# x 

# H 0.00% .'. Mid·Range •• 

## 18.4 18] '. 

## 0.63%

Hlgh- Range .48 48:1 0:1 

# J .0.21% Initial Values Final Values 312112008 843 312212008 746 Cylinder Analyzer Cal Systern Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias STACK C (3) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 103 0.0 0.0 1.6 3.33% 1.6 3.33% Upscale Gas 108 18.4 18.60 19.3 1.46% 19.7 2.29%
Initial Values Final Values 3121/2008 

## 851 3/22/2008 

## 756 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, Cal. Bias STACK 0 (4) Time (sec) PPM PPM PPM % of Span PPM % of Span Zero Gas 90 0.0 0 0.6 1.25% 1.0 2.08% Upscale Gas 88 18.4 18.7 18.8 0.21% 18.7 0.00%



# - System Callbrallon Bias - [(System Cal. Response - Analyzer Cal. Response) 

# I Span] x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) 

# I Span] x 100 

# S02 Drift, Percent of

span -0.83% -1.25%

Drift, Percent of

span

Drift, Percent of

span 0.00% 0.83%

Drift, Percent of

span 0.83% -0.21%

# BARR Engineering Company EPA METHOD 3A O 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/11/08 P. Rossmiller Cvlinder Serial No. Certified Value Zero Gas CC176437 0.0 Low-range

Mid-ranqe CC106732 

# 8.9 Hloh-ranqe 

# CC62111 21.0 ANALYZER CALIBRATION DATA Note: Difference must be less than 

# +1- 2 percent of span SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span Stack A - NOx(1) Analyzer Mod 

# 1 SN Model 200 Analyzer Span: 21.0 Zero Gas Low- Range Mid - Ran e High - Range Cylinder Value Analyzer Calibration Response Absolute Difference Difference as 

# % of Span Initial Values System Cal System Cal Response. Cal. Bias

PPM 

# % ofS an 0.1 Upscale Gas 20.8 System Calibration Bias 

# = [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span] x 100 Drift 

# =[(Final System Cal. Response -Initial System Cal Response) 

# 1 Span] x 100 

# O 2 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range**Mid-ran~e Hi~h-range**  

# Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/11/08 P. Rossmiller Cylinder Serial No. CC176437 CC106732 CC62111
ANALYZER CALIBRATION DATA Certified Value 0.0 8.9 21.0

Note: Difference must be less than +1- 2 percent of span Stack A - NOx(1) Analyzer Analyzer Mod 

# 1 SN Model 200 Cylinder Value Calibration Analyzer Span: 21.0 Response Zero Gas 0.0 0.1 Low- Range 0 Mid - Range 8.9 8.9 High - Range 21.0 21.0 Absolute Difference 0.1 0.0 0.0 0.0 

# EPA METHOD 3A O 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed +/- 5 percent of span. Drift cannot exceed +/- 7.5 percent of span Difference as

% of Span

0.24% 0.00% 0.19% 0.19% Initial Values Final Values Cylinder Analyzer Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, STACK A (1) Time (sec) PPM PPM PPM % of Span PPM Zero Gas 78 0.0 0.1 0.1 0.24% 0.1 Upscale Gas 76 21.0 21.0 20.8 -0.86% 20.6 System Calibration Bias 

# = [(System Cal. Response - Analyzer Cal. Response) / Span] x 100 Drift 

# = [(Final System Cal. Response -Initial System Cal Response) / Span) x 100 System Cal Cal. Bias % of Span

0.24% -1.71% 

# O 2 

# Drift,

Percent of

span 0.00% -0.86%

# BARR Engineering Company EPA METHOD 3A O 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/11/08 P. Rossmiller Cylinder Serial No. Certified Value Zero Gas CC176437 0.0 Low-rance

Mid-ranQe CC106732 

# 8.9 Hiqh-ranoe CC62111 21.0
ANALYZER CALIBRATION DATA Note: Difference must be less than +/- 2 percent of span SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +/- 5 percent of span. Drift cannot exceed 

# +/- 7.5 percent of span Stack A - NOx(1) Analyzer Mod / SN Model 200 Analyzer Span: 21.0 Zero Gas Low- Range Mid - Ran e High - Range Cylinder Value Analyzer Calibration Response Absolute Difference Difference as % of Span Initial Values System Cal System Cal Response, Cal. Bias

PPM 

# % ofS an 0.1 Upscale Gas 20.6 System Calibration Bias 

# =[(System Cal. Response - Analyzer Cal. Response) / Span] x 100 Drift 

# =[(Final System Cal. Response - Initial System Cal Response) / Span] x 100 Drift, Percent of 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-range High-range Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 

# 3/11/08 P. Rossmiller Cylinder Serial No. CC176437 CC106732 CC62111
ANALYZER CALIBRATION DATA Certified Value 0.0 8.9 21.0

Note: Difference must be less than 

# +1- 2 percent of span Stack A - NOx(1) Analyzer Analyzer Mod 

# 1 SN Model 200 Cylinder Value Calibration Analyzer Span: 21.0 Response Zero Gas 0.0 0.1 Low- Range 0 Mid - Range 8.9 8.9 High - Range 21.0 21.0 Absolute Difference 0.1 0.0 0.0 0.0 

# EPA METHOD 3A O 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span Difference as

% of Span

0.24% 0.00% 0.19% 0.19% Initial Values Final Values Cylinder Analyzer Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, STACK A (1) Time (sec) PPM PPM PPM % of Span PPM Zero Gas 78 0.0 0.1 0.1 0.24% 0.1 Upscale Gas 76 21.0 21.0 20.6 -1.71% 20.8 System Calibration Bias 

# = [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span] x 100 Drift 

# =[(Final System Cal. Response - Initial System Cal Response) 

# 1 Span] x 100 System Cal Cal. Bias % of Span

0.24% -0.76% Drift, Percent of

span 0.00% 0.95%

# BARR Engineering Company EPA METHOD 3A O 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Millal7-day Nox CEMS Fumace Scrubber Stack A-D 3/11/2008 - 3/12/08

P. Rossmiller Cylinder Serial No. Certified Value Zero Gas CC176437 0.0 

# tow-ranee

Mid-ranQe CC106732 8.9 Hlch-ranqe 

# CC62111 21.0 ANALYZER CALIBRATION DATA Note: Difference must be less than 

# +/- 2 percent of span SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +/- 5 percent of span. Drift cannot exceed 

# +/- 7.5 percent of span Stack A - NOx(1) Analyzer Mod / SN Model 200 Analyzer Span: 21.0 Zero Gas Low- Range Mid - Ran e High - Range Cylinder Value Analyzer Calibration Response Absolute Difference Difference as 

# % of Span STACKA 1 Zero Gas 78 Upscale Gas 76 System Calibration Bias 

# = [(System Cal. Response - Analyzer Cal. Response) / Span] x 100 Drift 

# =[(Final System Cal. Response -Initial System Cal Response) / Span] x 100 

# O2 

# Drift, Percent of 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-ranQe

Mid-ranQe High-range Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/11/2008 - 3/12/08

P. Rossmiller Cylinder Serial No. CC176437 CC106732 CC62111
ANALYZER CALIBRATION DATA Certified Value 0.0 8.9 21.0

Note: Difference must be less than 

# +/- 2 percent of span Stack A - NOx(1) Analyzer Analyzer Mod / SN Model 200 Cylinder Value Calibration Analyzer Span: 21.0 Response Zero Gas 0.0 0.1 Low- Range 0 Mid - Range 8.9 8.9 High - Range 21.0 21.0 Absolute Difference 0.1 0.0 0.0 0.0 

# EPA METHOD 3A O 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed 

# +/- 5 percent of span. Drift cannot exceed 

# +/- 7.5 percent of span Difference as % of Span

0.24% 0.00% 0.19% 0.19% Initial Values Final Values Cylinder Analyzer Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, STACK A (1) Time (sec) PPM PPM PPM % of Span PPM Zero Gas 78 0.0 0.1 0.1 0.24% 0.0 Upscale Gas 76 21.0 21.0 20.8 -0.76% 20.8 System Calibration Bias 

# = [(System Cal. Response - Analyzer Cal. Response) / Span] x 100 Drift 

# = [(Final System Cal. Response -Initial System Cal Response) / Span] x 100 System Cal Cal. Bias % of Span

-0.24% -0.76% 

# O2 

# Drift, Percent of

sjJan -0.48% 0.00%

# BARR Engineering Company EPA METHOD 3A O 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Miltal7-day Nox CEMS Furnace Scrubber Stack A-D 

# 3/12108 P. Rossmiller

Initial Values Final Values 3/12/2008 1237 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK A (1) 

## Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 78 0.0 0..1 .0.0 

# CO.:24"k Upscale Gas 76 >21.0 .·21.6 20.8 10.76% 

# ., Cylinder Serial No. Certified Value Zero Gas CC176437 0.0 Low-rance

Mid-ranoe CC106732 8.9 Hlqh-ranqe CC62111 21.0
ANALYZER CALIBRATION DATA Note: Difference must be less than +/- 2 percent of span Stack A - NOx(1) Analyzer Analyzer Mod / SN Model 200 Cylinder Value Calibration Absolute Difference as Analyzer Span: 21.0 Response Difference 

# % of Span Zero Gas 0.0 0.1 0.1 0.24% Low- Ranoe 0 0.0 0.00% Mid - Range 8.9 8.9 0.0 0.19% High - Range 21.0 21.0 0.0 0.19% SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +/- 5 percent of span. Drift cannot exceed 

# +/- 7.5 percent of span

System Calibration Bias 

# =[(System Cal. Response - Analyzer Cal. Response) / Span] x 100 Drift 

# =[(Final System Cal. Response -Initial System Cal Response) / Span] x 100 

# O 2 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-range High-range Mitlal7-day Nox CEMS Furnace Scrubber Stack A-D 

# 3/12108 P. Rossmiller Cylinder Serial No. CC176437 CC106732 CC62111
ANALYZER CALIBRATION DATA Certified Value 0.0 8.9 21.0

Note: Difference must be less than +/- 2 percent of span Stack A - NOx(1) Analyzer Analyzer Mod / SN Model 200 Cylinder Value Calibration Analyzer Span: 21.0 Response Zero Gas 0.0 0.1 Low- Ran!le 0 Mid - Range 8.9 8.9 High - Range 21.0 21.0 Absolute Difference 0.1 0.0 0.0 0.0 

# EPA METHOD 3A O 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed 

# +/- 5 percent of span. Drift cannot exceed 

# +/- 7.5 percent of span
Difference as



# % of Span

0.24% 0.00% 0.19% 0.19% Initial Values Final Values 3/12/2008 1237 Cylinder Analyzer Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, STACK A (1) Time (sec) PPM PPM PPM % of Span PPM Zero Gas 78 0.0 0.1 0.0 -0.24% Upscale Gas 76 21.0 21.0 20.8 -0.76% System Calibration Bias 

# = [(System Cal. Response - Analyzer Cal. Response) / Span] x 100 Drift 

# = [(Final System Cal. Response -Initial System Cal Response) / Span) x 100 System Cal Cal. Bias % of Span



# O

2 

## Drift,

Percent of

span

# BARR Engineering Company EPA METHOD 3A O 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mlttal7-day Nox CEMS Furnace Scrubber Stack A-D 3/12/08 P. Rossmiller Cylinder Serial No. Certified Value Zero Gas CC176437 0.0 low-ranae

Mid-ranae CC106732 8.9 

# Hioh-rance CC62111 21.0
ANALYZER CALIBRATION DATA Note: Difference must be less than +/- 2 percent of span SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed +/- 5 percent of span. Drift cannot exceed +/- 7.5 percent of span Stack A - NOx(1) Analyzer Analyzer Mod / SN Model 200 Cylinder Value Calibration Absolute Difference as Analyzer Span: 21.0 Response Difference % of Span Zero Gas 0.0 0.1 0.1 0.24% Low- Range 0 0.0 0.00% Mid - Range 8.9 8.9 0.0 n 100/. 

## High - Range 21.0 21.0 0.0 0.19% Cylinder Value Final Values 3/13/2008 1114 System Cal System Cal Response, Cal. Bias

PPM % ofS an 

# 0.1 20.6 Drift, Percent of 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas low-ranqe

Mid-range HiQh-ranQe Mlttal7-day Nox CEMS Furnace Scrubber Stack A-D 

# 3/12/08 P. Rossmiller Cylinder Serial No. CC176437 CC106732 CC62111
ANALYZER CALIBRATION DATA Certified Value 0.0 8.9 21.0

Note: Difference must be less than 

# +1- 2 percent of span Stack A - NOx(1) Analyzer Analyzer Mod 

# 1 SN Model 200 Cylinder Value Calibration Analyzer Span: 21.0 Response Zero Gas 0.0 0.1 Low- Range 0 Mid - Range 8.9 8.9 High - Range 21.0 21.0 Absolute Difference 0.1 0.0



# . 0.0 .' 

# 0.0 

# EPA METHOD 3A O 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span Difference as

% of Span

0.24% 0.00%

. 0.19% 0.19% Initial Values Final Values 

# 3/12/2008 1237 

# 3/13/2008 Cylinder Analyzer Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, STACK A (1) Time (sec) PPM PPM PPM % of Span PPM Zero Gas 78 0.0 0.1 0.0 -0.24% 0.1 Upscale Gas 76 21.0 21.0 20.8 -0.76% 20.6



# - System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span] x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) 

# 1 Span] x 100 1114 System Cal Cal. Bias % of Span

0.24% -1.71% Drift, Percent of

span 0.48% -0.95%

# BARR Engineering Company EPA METHOD 3A O 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mitlal7-day Nox CEMS Furnace Scrubber Stack A-D 3/12/08 P. Rossmiller Cvlinder Serial No. Certified Value Zero Gas CC176437 0.0 Low-rance

Mid-range CC106732 8.9 HiQh-range CC62111 21.0
ANALYZER CALIBRATION DATA Note: Difference must be less than +/- 2 percent of span SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed +/- 5 percent of span. Drift cannot exceed +/- 7.5 percent of span Stack A - NOx(1) Analyzer Analyzer Mod / SN Model 200 Cylinder Value Calibration Absolute Difference as Analyzer Span: 21.0 Response Difference % of Span Zero Gas 0.0 0.1 0.1 

# . 0.24% Low- Rance 0 0.0 0.00% Mid - Range 8.9 8.9 0.0 I 0.19% High - Range 21.0 21.0 . 0.0 0.19% STACKA 1 Cylinder Value Analyzer Cal Response, Initial Values 3/13/2008 System Cal System Cal Response, Cal. Bias

PPM Final Values 3/14/2008 739 System Cal System Cal Response, Cal. Bias

PPM Drift, Percent of 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-range High-range Miltal7-day Nox CEMS Furnace Scrubber Stack A-D 3/12/08 

# P. Rossmiller Cylinder Serial No. CC176437 CC106732 CC62111
ANALYZER CALIBRATION DATA Certified Value 0.0 8.9 21.0

Note: Difference must be less than 

# +1- 2 percent of span Stack A - NOx(1) Analyzer Analyzer Mod 

# 1SN Model 200 Cylinder Value Calibration Analyzer Span: 21.0 Response Zero Gas 0.0 0.1 Low- Ran!le 0 Mid - Range 8.9 8.9 High - Range 21.0 21.0 Absolute Difference 0.1 0.0 0.0 0.0 

# EPA METHOD 3A O 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span
Difference as % of Span

0.24% 0.00% 0.19% 0.19% Initial Values Final Values 3/13/2008 

# 1114 3/14/2008 

# Cylinder Analyzer Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, STACK A (1) Time (sec) PPM PPM PPM % of Span PPM Zero Gas 78 0.0 0.1 0.1 0.24% 0.1 Upscale Gas 76 21.0 21.0 20.6 -1.71% 20.6 System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span) x 100 Drift 

# =[(Final System Cal. Response -Initial System Cal Response) 

# 1 Span) x 100 739 System Cal Cal. Bias % of Span

0.24% -1.71% Drift, Percent of

span 0.00% 0.00%

# BARR Engineering Company EPA METHOD 3A O 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mittal 7-day Nox CEMS Furnace Scrubber Stack A-D 3/12/08 P. Rossmiller Cylinder Serial No. Certified Value Zero Gas CC176437 0.0 Low-range

Mid-range CC106732 8.9 High-range CC62111 21.0 ANALYZER CALIBRATION DATA Note: Difference must be less than 

# +/- 2 percent of span SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +/- 5 percent of span. Drift cannot exceed 

# +/- 7.5 percent of span Initial Values Final Values 3/14/2008 739 3/14/2008 2151 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK A (1) Time (sec) PPM PPM PPM 

# % of Span PPM 

# % of Span span Zero Gas 78 0.0 .0;1 0.1 0.24%' 0.0

# ~().24% <0.480/0 Upscale Gas 76 21.0 21.() 20.6 

# i"1.71% 20.8**.~(),76oJ';** 

# 0.95% Stack A - NOx(1) Analyzer Mod / SN Model 200 Analyzer Span: 21.0 Zero Gas Low- Ran e Mid - Range High - Range Cylinder Value Analyzer Calibration Response Absolute Difference Difference as 

# % of Span

System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) / Span) x 100 Drift 

# =[(Final System Cal. Response - Initial System Cal Response) / Span) x 100 

# O 2 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-range High-range Millal 7-day Nox CEMS Furnace Scrubber Stack A-D 3/12/08 P. Rossmiller Cylinder Serial No. CC176437 CC106732 CC62111
ANALYZER CALIBRATION DATA Certified Value 0.0 8.9 21.0

Note: Difference must be less than 

# +/- 2 percent of span Stack A - NOx(1) Analyzer Analyzer Mod / SN Model 200 Cylinder Value Calibration Analyzer Span: 21.0 Response Zero Gas 0.0 0.1 Low- Range 0 Mid - Range 8.9 8.9 High - Range 21.0 21.0 Absolute Difference 0.1 0.0 0.0 0.0 

# EPA METHOD 3A O 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed 

# +/- 5 percent of span. Drift cannot exceed 

# +/- 7.5 percent of span
Difference as % of Span

0.24% 0.00% 0.19% 0.19% Initial Values Final Values 3/14/2008 739 3/14/2008 Cylinder Analyzer Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, STACK A (1) Time (sec) PPM PPM PPM % of Span PPM Zero Gas 78 0.0 0.1 0.1 0.24% 0.0 Upscale Gas 76 21.0 21.0 20.6 -1.71% 20.8 System Cahbralion Bias - [(System Cal. Response - Analyzer Cal. Response) / Span) x 100 Drift 

# =[(Final System Cal. Response - Initial System Cal Response) / Span) x 100 2151 System Cal Cal. Bias % of Span

-0.24% -0.76% 

# O 2 

# Drift,

Percent of

span -0.48% 0.95%

# BARR Engineering Company EPA METHOD 3A O2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/16/08 AGA Cylinder Serial No. Certified Value Zero Gas CC176437 0.0 Low-range

Mid-range CC106732 8.9 Hloh-rance CC62111 21.0
ANALYZER CALIBRATION DATA Note: Difference must be less than 

# +/- 2 percent of span SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +/- 5 percent of span. Drift cannot exceed 

# +/- 7.5 percent of span Stack A - NOx(1) Analyzer Mod / SN Model 200 Analyzer Span: 21.0 Zero Gas Low- Ran e Mid - Range High - Range Cylinder Value Analyzer Calibration Response 0.0 9.0 21.0 Absolute Difference Difference as 

# % of Span Drift. Percent of 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low- ra llge

Mid-range HiQh-ranQe Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/16/08 

# AGA Cylinder Serial No. CC176437 CC106732 CC62111
ANALYZER CALIBRATION DATA Certified Value 0.0 8.9 21.0

Note: Difference must be less than 

# +1- 2 percent of span Stack A - NOx(1) Analyzer Analyzer Mod 

# 1 SN Model 200 Cylinder Value Calibration Analyzer Span: 21.0 Response Zero Gas 0.0 0.0 Low- Range 0 Mid - Range 8.9 9.0 High - Range 21.0 21.0 Absolute Difference 0.0 0.0 0.1 0.0 

# EPA METHOD 3A O2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span Difference as

% of Span

0.00% 0.00% 0.48% 0.00% Initial Values Final Values 3/16/2008 

# 2130 3/17/2008 

# Cylinder Analyzer Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, STACK A (1)**Time~sec)** 

# PPM PPM PPM % of Span PPM Zero Gas 78 0.0 0.0 0.1 0.48% 0.1 Upscale Gas 76 21.0 21.0 20.7 -1.43% 20.7 System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span) x 100 Drift 

# = [(Final System Cal. Response -Initial System Cal Response) 

# 1Span) x 100 941 System Cal Cal. Bias % of Span

0.48% -1.43% Drift, Percent of

span 0.00% 0.00%

# BARR Engineering Company EPA METHOD 3A O 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mittal 7-day Nox CEMS Furnace Scrubber Stack A-D 3/16/08 AGA Cylinder Serial No. Certified Value Zero Gas CC176437 0.0 

# Low-rance

Mid-range CC106732 8.9 

# Hloh-ranqe CC62111 21.0 ANALYZER CALIBRATION DATA Note: Difference must be less than +/- 2 percent of span SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed +/- 5 percent of span. Drift cannot exceed +/- 7.5 percent of span

System Calibration Bias 

# =[(System Cal. Response - Analyzer Cal. Response) / Span] x 100 Drift 

# =[(Final System Cal. Response - Initial System Cal Response) / Span] x 100 Drift, Percent of



# O

2 

# 0.1 Final Values

20.4 3/18/2008 828 System Cal System Cal Response, Cal. Bias

PPM Initial Values 3/17/2008 System Cal Response,

PPM Cylinder Value STACKA 1 Zero Gas Upscale Gas Difference as % of Span Absolute Difference Analyzer Calibration Response Cylinder Value
Zero Gas Mid - Range Low- Ran e High - Range Stack A - NOx(1) Analyzer Mod / SN Model 200 Analyzer Span: 21.0 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-range High-range Mittal 7-day Nox CEMS Furnace Scrubber Stack A-D 3/16/08 AGA CyJinder Serial No. CC176437 CC106732 CC62111
ANALYZER CALIBRATION DATA Certified Value 0.0 8.9 21.0

Note: Difference must be less than 

# +/- 2 percent of span Stack A - NOx(1) Analyzer Analyzer Mod / SN Model 200 Cylinder Value Calibration Analyzer Span: 21.0 Response Zero Gas 0.0 0.0 Low- Range 0 Mid - Range 8.9 9.0 High - Range 21.0 21.0 Absolute Difference 0.0 0.0 0.1 0.0 

# EPA METHOD 3A O 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed 

# +/- 5 percent of span. Drift cannot exceed 

# +/- 7.5 percent of span Difference as % of Span

0.00% 0.00% 0.48% 0.00% Initial Values Final Values 3/17/2008 941 3/18/2008 Cylinder Analyzer Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, STACK A (1) Time (sec) PPM PPM PPM % of Span PPM Zero Gas 78 0.0 0.0 0.1 0.48% 0.1 Upscale Gas 76 21.0 21.0 20.7 -1.43% 20.4 System Calibration Bias 

# = [(System Cal. Response - Analyzer Cal. Response) / Span] x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) 

# I Span] x 100 828 System Cal Cal. Bias % of Span

0.48% -2.86% 

# O 2 

# Drift,

Percent of

span 0.00% -1.43%

# BARR Engineering Company EPA METHOD 3A O 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mitlal7-day Nox CEMS Furnace Scrubber Stack A-D 3/18/08 

# AGA Cvlinder Serial No. Certified Value Zero Gas CC176437 0.0 Low-range

Mid-range CC106732 8.9 High-range CC62111 21.0



# O 2 

# SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed +1-5 percent of span. Drift cannot exceed +1-7.5 percent of span

System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span] x 100 Drift '" [(Final System Cal. Response - Initial System Cal Response) 

# 1 Span] x 100 Initial Values Final Values 3/1812008 

# 936 3/19/2008 

# 756 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK A (1) 

# Time (sec) PPM PPM PPM % of Soan PPM % of Soan soan Zero Gas 78 0.0 ·0.0 0.1 .0.48% .0.0· 

# I·i·.··o.obblo •.. 0.480/0 Upscale Gas 76 ·21.0 21.0 20.8 -0:950/0 ·20.8 (.. 0,950/0 0.00% ANALYZER CALIBRATION DATA N'ff b I ote: DI erence must e ess than 

# + - 2 percent of soan v"O'£UUO 

# Stack A - NOx(1) Analyzer Analyzer Mod 1 SN Model 200 Cylinder Value Calibration Absolute Difference as Analyzer Span: 21.0 Response Difference % of Span Zero Gas 0.0 0.0 0.0 •. 0.00°"'; Low- Rance 0 

# i 

# Ii 0.0. 0.00% Mid - Range 8.9 9.0 0;1 0;33°/" High - Range 21.0 21.0 0.0 0.00% 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-range High-range Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/18/08 

# AGA Cylinder Serial No. CC176437 CC106732 CC62111
ANALYZER CALIBRATION DATA Certified Value 0.0 8.9 21.0

N'ff b I ote: DI erence must e ess than 

# + - 2 percent of sjJ8n "/IO/"'UUO 

# Stack A - NOx(1) Analyzer Analyzer Mod 

# I SN Model 200 Cylinder Value Calibration Analyzer Span: 21.0 Response Zero Gas 0.0 0.0 Low-**Ran~e** 

# 0 Mid - Range 8.9 9.0 High - Range 21.0 21.0 Absolute Difference 0.0 0.0 0.1 0.0 

# EPA METHOD 3A O 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed +/- 

# 5 percent of span. Drift cannot exceed +/- 

# 7.5 percent of span Difference as % of Span

0.00% 0.00% 0.33% 0.00% Initial Values Final Values 3/18/2008 936 3/19/2008 

# Cylinder Analyzer Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, STACK A (1) Time (sec) PPM PPM PPM % of Span PPM Zero Gas 78 0.0 0.0 0.1 0.48% 0.0 Upscale Gas 76 21.0 21.0 20.8 -0.95% 20.8 System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span] x 100 Drift '" [(Final System Cal. Response - Initial System Cal Response) 

# 1 Span] x 100 756 System Cal Cal. Bias % of Span

0.00% -0.95% 

# O 2 

# Drift,

Percent of

span -0.48% 0.00%

# BARR Engineering Company EPA METHOD 3A O 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Miltal7-day Nox CEMS Fumace Scrubber Stack A-D 3118108 AGA Cylinder Serial No. Certified Value Zero Gas CC176437 0.0 Low-range

Mid-range CC106732 8.9 High-range CC62111 21.0 SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed +1-5 percent of span. Drift cannot exceed +/- 7.5 percent of span

System Cahbralion Bias - [(System Cal. Response - Analyzer Cal. Response) / Span) x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) / Span) x 100 Initial Values Final Values 311812008 936 3/19/2008 756 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK A (1) Time (sec) PPM PPM PPM 

# % of Span PPM 

# % of Span span Zero Gas 78 ().O , :O,() 0.1 ().4S% 0.0 ().OO%' cO:48% Upscale Gas 76 '21]0 -v- 

# ,1;21.0 20.8 00.95% 20.8 '-0.95% 0.00%



# - ANALYZER CALIBRATION DATA 

# N I

ote: Difference must be ess than +/- 2 percent of span Stack A - NOx(1) Analyzer Analyzer Mod I SN Model 200 Cylinder Value Calibration Absolute Difference as Analyzer Span: 21.0 Response Difference % of Span Zero Gas 0.0 0.0 0.0 O.OC Low- Range 0 0.0 Mid - Range 8.9 9.0 0.1 0.33 High - Range 21.0 21.0 0.0 0.00 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-range High-range Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3118108 AGA Cylinder Serial No. CC176437 CC106732 CC62111
ANALYZER CALIBRATION DATA Certified Value 0.0 8.9 21.0



# N I

ote: Difference must be ess than +/- 2 percent of sjJ3n vl'O'''UUO 

# Stack A - NOx(1) Analyzer Analyzer Mod I SN Model 200 Cylinder Value Calibration Analyzer Span: 21.0 Response Zero Gas 0.0 0.0 Low- Range 0 Mid - Range 8.9 9.0 High - Range 21.0 21.0 Absolute Difference 0.0 0.0 0.1 0.0 

# EPA METHOD 3A O 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed +1- 5 percent of span. Drift cannot exceed +/- 7.5 percent of span Difference as

% of Span

0.00% 0.00% 0.33% 0.00% .' Initial Values Final Values 311812008 936 3/19/2008 Cylinder Analyzer Cal Systern Cal Systern Cal System Cal Response Value Response, Response, Cal. Bias Response, STACK A (1) Tirne (sec) PPM PPM PPM % of Span PPM Zero Gas 78 0.0 0.0 0.1 0.48% 0.0 Upscale Gas 76 21.0 21.0 20.8 -0.95% 20.8



# - System Calibralion Bias - [(System Cal. Response - Analyzer Cal. Response) / Span) x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) / Span) x 100 756 System Cal Cal. Bias % of Span

0.00% -0.95% Drift, Percent of

span -0.48% 0.00%

# BARR Engineering Company EPA METHOD 3A O2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/20/08 AGA

Initial Values Final Values 3/19/2008 756 3/20/2008 754 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACKA(1) Time (sec) PPM PPM PPM 

# % of Span PPM 

# % of Span span Zero Gas 78 0.0 0.0. 0.0. 0.00%: 0.0 /0:00% 0.00% Upscale Gas 76 2{0 21.0 20.8 '"0:95% 21.0 'O!19% )1:14% Cylinder Serial No. Certified Value Zero Gas CC176437 0.0 

# tow-ranee

Mid-ranQe CC106732 8.9 Hiqh-ranqe CC62111 21.0
ANALYZER CALIBRATION DATA Note: Difference must be less than +/- 2 percent of span Stack A - NOx(1) Analyzer Analyzer Mod / SN Model 200 Cylinder Value Calibration Absolute Difference as Analyzer Span: 21.0 Response Difference % 

## of Span Zero Gas 0.0 0.0 

# I 0.0 0.00' 

# , Low- Rance 0 0.0 0.00' Mid - Range 8.9 9.0 0.1 0.33' High - Range 21.0 21.0 0.0 0.00' SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +/- 5 percent of span. Drift cannot exceed 

# +/- 7.5 percent of span

System Catibration Bias 

# = [(System Cal. Response - Analyzer Cal. Response) / Span] x 100 Drift 

# =[(Final System Cal. Response - Initial System Cal Response) / Span] x 100 

# 02 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-range High-range Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 

# 3/20/08 AGA Cylinder Serial No. CC176437 CC106732 CC62111
ANALYZER CALIBRATION DATA Certified Value 0.0 8.9 21.0

Note: Difference must be less than +/- 

# 2 percent of span OJ"O'.'UUO 

# Stack A - NOx(1) Analyzer Analyzer Mod 

# 1 SN Model 200 Cylinder Value Calibration Analyzer Span: 21.0 Response Zero Gas 0.0 0.0 Low- Range 0 Mid - Range 8.9 9.0 High - Range 21.0 21.0 Absolute Difference 0.0 0.0 0.1 0.0 

# EPA METHOD 3A O2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +/- 7.5 percent of span Difference as

% 

# of Span

0.00% 0.00% 0.33% 0.00%' Initial Values Final Values 

# 3/19/2008 756 

# 3/20/2008 Cylinder Analyzer Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, STACK A (1) Time (sec) PPM PPM PPM % of Span PPM Zero Gas 78 0.0 0.0 0.0 0.00% 0.0 Upscale Gas 76 21.0 21.0 20.8 -0.95% 21.0 System Calibration Bias 

# = [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span] x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) 

# 1 Span] x 100 754 System Cal Cal. Bias 

# % of Span

0.00% 0.19% 

# O 2 

# Drift,

Percent of

span 0.00% 1.14%

# BARR Engineering Company EPA METHOD 3A O 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/20/06 

# AGA Cylinder Serial No. Certified Value Zero Gas CC176437 0.0 

# Low-rance

Mid-ranae CC106732 6.9 

# Hioh-ranqe CC62111 21.0

Drift, Percent of



# O

2 

# Final Values 3/21/2006 641 

# System Cal System Cal Response, Cal. Bias

PPM % ofS an 0.1 Cylinder Value SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span 

# t f ANALYZER CALIBRATION DATA N t D'ff t b I th

oe: I 

# erence mus e ess an 

# + - 2 percen 0 

# span Stack A - NOx(1) Analyzer Analyzer Mod 

# 1 SN Model 200 Cylinder Value Calibration Absolute Difference as Analyzer Span: 21.0 Response Difference % of Span Zero Gas 0.0 0.0 0.0 0.00% low- Range 0 0.0 0.00% Mid - Range 6.9 9.0 I 

# 0.1 0.33% High - Range 21.0 21.0 0.0 0.00% 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-ranQe

Mid-ranQe HiQh-ranQe Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 

# 3/20/06 AGA Cylinder Serial No. CC176437 CC106732 CC62111
ANALYZER CALIBRATION DATA Certified Value 0.0 6.9 21.0

N t D'ff t b I th

oe: I 

# erence mus e ess 

# t f an 

# + - 2 percen 0 

# span .;)"o,.<;uuo 

# Stack A - NOx(1) Analyzer Analyzer Mod 

# 1 SN Model 200 Cylinder Value Calibration Analyzer Span: 21.0 Response Zero Gas 0.0 0.0 low- Range 0 Mid - Range 6.9 9.0 High - Range 21.0 21.0 Absolute Difference 0.0 0.0 0.1 0.0 

# EPA METHOD 3A O 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span Difference as % of Span

0.00% 0.00% 0.33% 0.00% Initial Values Final Values 

# 3/20/2006 754 

# 3/21/2006 Cylinder Analyzer Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, STACK A (1) Time (sec) PPM PPM PPM % of Span PPM Zero Gas 76 0.0 0.0 0.0 0.00% 0.1 Upscale Gas 76 21.0 21.0 21.0 0.19% 21.0



# - System Calibralion Bias - [(System Cal. Response - Analyzer Cal. Response) 1 Span) x 100 Drift 

# = [(Final System Cal. Response -Initial System Cal Response) 1 Span) x 100 641 System Cal Cal. Bias % of Span

0.48% 0.00% 

# O 2 

# Drift,

Percent of

span 0.48% -0.19%

# BARR Engineering Company EPA METHOD 3A O 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mitlal 7-day Nox CEMS Furnace Scrubber Stack A-D 

# 3/20/08 AGA Cylinder Serial No. Certified Value Zero Gas CC176437 .0.0 Low-range

Mid-ranoe CC106732 8.9 

# Hloh-ranue CC62111 21.0
ANALYZER CALIBRATION DATA Note: Difference must be less than 

# +/- 2 percent of span Stack A - NOx(1) Analyzer Analyzer Mod / SN Model 200 Cylinder Value Calibration Absolute Difference as Analyzer Span: 21.0 Response Difference % of Span Zero Gas 0.0 0.0 0.0 O.OC%
. Low- Rance 0 0.0 n 

# vc % Mid - Range 8.9 9.0 

# , 0.1 

# . o.**3~%** High - Range 21.0 . 21.0 0.0 

# o. OC% SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +/- 5 percent of span. Drift cannot exceed 

# +/- 7.5 percent of span
Cylinder Value STACKA 1 Zero Gas Drift, Percent of 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-ranqe Hiqh-ranqe Mittal 7 -day Nox CEMS Furnace Scrubber Stack A-D 

# 3/20/08 AGA Cylinder Serial No. CC176437 CC106732 CC62111
ANALYZER CALIBRATION DATA Certified Value 0.0 8.9 21.0

Note: Difference must be less than 

# +1- 2 percent of span ->1 OILUUC 

# Stack A - NOx(1) Analyzer Analyzer Mod 

# 1 SN Model 200 Cylinder Value Calibration Analyzer Span: 21.0 Response Zero Gas 0.0 0.0 Low- Range 0 Mid - Range 8.9 9.0 High - Range 21.0 . 21.0 Absolute Difference 0.0 0.0 0.1 0.0 

# EPA METHOD 3A O 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed 

# +/- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span Difference as

% of Span

0.00% 0.00% ·'0.33% 0.00% Initial Values Final Values 

# 3/21/2008 841 

# 3/2212008 Cylinder Analyzer Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, STACK A (1) Time (sec) PPM PPM PPM % of Span PPM Zero Gas 78 0.0 0.0 0.1 0.48% 0.1 Upscale Gas 76 21.0 21.0 21.0 0.00% 21.0



# - System Callbralion Bias - [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span] x 100 Drift 

# = [(Final System Cal. Response -Initial System Cal Response) 

# 1 Span] x 100 754 System Cal Cal. Bias % of Span

0.48% 0.00% Drift, Percent of

span 0.00% 0.00%

# BARR Engineering Company EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION Project Sample loco Date Operators Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/11/08 P. Rossmiller Cvlinder Serial No. Certified Value Zero Gas CC176437 0.0 low-range

Mid-ranee CC62111 5.05 Hiqh-ranqe CC106732 8.9
ANALYZER CALIBRATION DATA Note: Difference must be less than +/- 2 percent of span SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +/- 5 percent of span. Drift cannot exceed 

# +/- 7.5 percent of span Stack A - NOx(1) Analyzer Mod / SN Model 200 Analyzer Span: 8.9 Cylinder Value Analyzer Calibration Response Absolute Difference Difference as 

# % of Span

U scale Gas System Calibration Bias 

# =[(System Cal. Response - Analyzer Cal. Response) / Span) x 100 Drift 

# =[(Final System Cal. Response - Initial System Cal Response) / Span) x 100 Drift, Percent 01 

# BARR Engineering Company Project Sample loco Date Operators

Zero Gas low-range

Mid-range High-range Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/11/08 P. Rossmiller Cylinder Serial No. CC176437 CC62111 CC106732
ANALYZER CALIBRATION DATA Certified Value 0.0 5.05 8.9

Note: Difference must be less than +/- 

# 2 percent of span Stack A - NOx(1) Analyzer Analyzer Mod / SN Model 200 Cylinder Value Calibration Analyzer Span: 8.9 Response Zero Gas 0.0 0.0 low- Range 0 Mid- Ra[lge 5.05 5.0 High - Range 8.9 8.9 Absolute Difference



# . 0.0 0.0 0.1 0.0 

# EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed 

# +/- 5 percent of span. Drift cannot exceed 

# +/- 7.5 percent of span Difference as % of Span

0.00% 0.00% 0.79% 0.22% Initial Values Final Values Cylinder Analyzer Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, STACK A (1) Time (sec) PPM PPM PPM % of Span PPM Zero Gas 78 0.0 0.0 0.1 0.67% 0.2 Upscale Gas 76 5.05 5.0 4.9 -0.45% 4.6 System Calibration Bias 

# = [(System Cal. Response - Analyzer Cal. Response) / Span) x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) / Span) x 100 System Cal Cal. Bias**%ofS~an** 

# 2.25% -2.02% Drift, Percent of

SfJan 1.57% -1.57%

# BARR Engineering Company EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mitlal7-day Nox CEMS Furnace Scrubber Stack A-D 

# 3/11/08 P. Rossmiller Cylinder Serial No. Certified Value Zero Gas CC176437 0.0 Low-rance

Mid-ranqe CC62111 5.05 

# Hiqh-ranqe CC106732 8.9
ANALYZER CALIBRATION DATA Note: Difference must be less than 

# +1- 2 percent of span SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span Stack A - NOx(1) Analyzer Mod 

# 1 SN Model 200 Analyzer Span: 8.9 Zero Gas Low- Range Mid - Ran e High - Range Cylinder Value Analyzer Calibration Response Absolute Difference Difference as 

# % of Span Cylinder Value STACKA 1 Zero Gas Upscale Gas 4.8 System Calibration Bias 

# = [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span) x 100 Drift 

# =[(Final System Cal. Response - Initial System Cal Response) 

# 1 Span) x 100 Drift. Percent of 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-range High-range Mittal 7-day Nox CEMS Furnace Scrubber Stack A-D 

# 3/11/08 P. Rossmiller Cylinder Serial No. CC176437 CC62111 CC106732
ANALYZER CALIBRATION DATA Certified Value 0.0 5.05 8.9

Note: Difference must be less than 

# +1- 2 percent of span Stack A - NOx(1) Analyzer Analyzer Mod 

# 1SN Model 200 Cylinder Value Calibration Analyzer Span: 8.9 Response Zero Gas 0.0, 0.0 Low- Range 0 Mid - Range 5.05 5.0 High - Range 8.9 , 8.9 Absolute Difference 0.0 0.0 0.1 0.0 

# EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span Difference as % of Span

0.00% 0.00% 0.79% 0.22% Initial Values Final Values Cylinder Analyzer Cal System Cal System Cal System Cal Response Value Response, Response. Cal. Bias Response, STACK A (1) Time (sec) PPM PPM PPM % of Span PPM Zero Gas 78 0.0 0.0 0.2 '2.25% 0.0 Upscale Gas 76 5.05 5.0 4.8 -2.02% 5.0 System Calibration Bias 

# = [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span) x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) 

# 1 Span) x 100 System Cal Cal. Bias % of Span

0.00% 0.22% Drift. Percent 01

span -2.25% 2.25%

# BARR Engineering Company EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/11/2006 - 3/12/06

P. Rossmiller Cvlinder Serial No. Certified Value Zero Gas CC176437 0,0 Low-raMe

Mid-ranee CC62111 5.05 Hioh-ranoe CC106732 8.9 ANALYZER CALIBRATION DATA Note: Difference must be less than +/- 2 percent of span SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed +/- 5 percent of span. Drift cannot exceed +/- 7.5 percent of span StackA- NOx(1) Analyzer Mod / S.N Model 200 Analyzer Span: 8.9 Zero Gas Low- Range Mid - Ran e High - Range Cylinder Value Analyzer Calibration Response Absolute Difference Difference as % of Span
Upscale Gas System Calibration Bias 

# =[(System Cal. Response - Analyzer Cal. Response) / Span) x 100 Drift 

# =[(Final System Cal. Response -Initial System Cal Response) / Span) x 100 CO 2 

# Drift. Percent of 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-raiii:le

Mid-ranee Hioh-ranoe Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/11/2006 - 3/12/06

P. Rossmiller Cylinder Serial No. CC176437 CC62111 CC106732
ANALYZER CALIBRATION DATA Certified Value 0.0 5.05 8.9

Note: Difference must be less than 

# +/- 2 percent of span StackA- NOx(1) Analyzer Analyzer Mod / S.N Model 200 Cylinder Value Calibration Analyzer Span: 8.9 Response Zero Gas 0.0 0.0 Low- Range 0 Mid - RanQe 5.05 5.0 High - Range 8.9 8.9 Absolute Difference

" 

# 0.0 0.0 0.1

. 0.0 

# EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed 

# +/- 5 percent of span. Drift cannot exceed 

# +/- 7.5 percent of span Difference as

% of Span

0.00% 0.00% 0.79% 0.22% Initial Values Final Values Cylinder Analyzer Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, STACK A (1) Time (sec) PPM PPM PPM % of Span PPM Zero Gas 78 0.0 0.0 0.0 0.00% 0.0 Upscale Gas 76 5.05 5.0 5.0 0.22% 4.9 System Calibration Bias 

# =[(System Cal. Response - Analyzer Cal. Response) / Span) x 100 Drift 

# = [(Final System Cal. Response -Initial System Cal Response) / Span) x 100 System Cal Cal. Bias % of Span

0.00% -0.90% CO 2 

# Drift. Percent of

span 0.00% -1.12%

# BARR Engineering Company EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Millal7-day Nox CEMS Furnace Scrubber Stack A-D 3/12/08 P. Rossmiller Cylinder Serial No. Certified Value Zero Gas CC176437 0.0 Low-rance

Mid-ranQe CC62111 5.05 Hlqh-ranqe CC106732 8.9
ANALYZER CALIBRATION DATA Note: Difference must be less than +/- 2 percent of span SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +/- 5 percent of span. Drift cannot exceed 

# +/- 7.5 percent of span

CO 2 

## System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) / Span] 

# x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) / Span] x 100 Initial Values Final Values 3/12/2008 1237 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK A (1) Time (sec) PPM PPM PPM

# o/~ PPM 

# % of Span span Zero Gas 78 0.0 0.0 0.0 Upscale Gas 76 5.05 5.0 4.9



# - Stack A - NOx(1) Analyzer Analyzer Mod / SN Model 200 Cylinder Value Calibration Absolute Difference as Analyzer Span: 8.9 Response Difference 

# % of Span Zero Gas 0.0 0.0 0.0 [,0,000;.,2) Low- Rance 0 

# D.O. ··.0.00"/. Mid - Range 5.05 5.0 

# oJ 0.79% High - Range 8.9 8.9 ·>:0.0> 0.22% 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-range High-range MiUal7-day Nox CEMS Furnace Scrubber Stack A-D 3/12/08 

# P. Rossmiller Cylinder Serial No. CC176437 CC62111 CC106732
ANALYZER CALIBRATION DATA Certified Value 0.0 5.05 8.9

Note: Difference must be less than +/- 

# 2 percent of span Stack A - NOx(1) Analyzer Analyzer Mod 

# 1 SN Model 200 Cylinder Value Calibration Analyzer Span: 8.9 Response Zero Gas 0.0 0.0 Low- Range 0 Mid - Range 5.05 5.0 High - Range 8.9 8.9 Absolute Difference 0.0 0.0 0.1 0.0 

# EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span Difference as

% of Span

0.00% 0.00% 0.79% 0.22% Initial Values Final Values 3/12/2008 

# 1237 Cylinder Analyzer Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, STACK A11) Time (sec), PPM PPM PPM % of Span PPM Zero Gas 78 0.0 0.0 0.0 0.00% Upscale Gas 76 " 

# 5.05 5.0 4.9 -0.90% .,



# - System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span] 

# x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) 

# 1 Span] x 100 System Cal Cal. Bias % of Span

CO 2 

# Drift, Percent of

span

# BARR Engineering Company EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/12/08 P. Rossmiller

Initial Values Final Values 3/12/2008 .1237 3/13/2008 1114 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK A (1) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 78 0:0 ll.O ·'0.0·

# o.boo/~ 0.1 1:120/. 

# 11\.12°/0' Upscale Gas 76 5.05 

# 5:0 Ii 4.9 ····-ll.90% 5.0 0:22% 1:12% Cylinder Serial No. Certified Value Zero Gas CC176437 0.0 Low-rance

Mid-ranqe CC621.11 5.05 

# Hloh-rance CC106732 8.9
ANALYZER CALIBRATION DATA Note: Difference must be less than 

# +/- 2 percent of span Stack A - NOx(1) Analyzer Analyzer Mod / SN Model 200 Cylinder Value Calibration Absolute Difference as Analyzer Span: 8.9 Response Difference % of Span Zero Gas 0.0 0.0 0.0 0.00% Low- Rance 0 0.0 0.00% Mid - Range 5.05 5.0 0.1 0.79% High - Range 8.9 8.9 0.0 . 0.22% SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +/- 5 percent of span. Drift cannot exceed 

# +/- 7.5 percent of span

System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) / Span] x 100 Drift 

# =[(Final System Cal. Response - Initial System Cal Response) / Span] x 100 CO 2 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-range High-range Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/12/08 

## P. Rossmiller Cylinder Serial No. CC176437 CC62111 CC106732
ANALYZER CALIBRATION DATA Certified Value 0.0 5.05 8.9

Note: Difference must be less than 

# +1- 2 percent of span Stack A - NOx(1) Analyzer Analyzer Mod 

# I SN Model 200 Cylinder Value Calibration Analyzer Span: 8.9 Response Zero Gas 0.0 0.0 Low- Range 0 Mid - Range 5.05 5.0 High - Range 8.9 8.9 Absolute Difference 0.0 0.0 0.1 0.0 

# EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span
Difference as % of Span

0.00% 0.00% 0.79% 0.22% Initial Values Final Values 3/12/2008 

## 1237 3/13/2008 

## Cylinder Analyzer Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, STACK A (1) Time (sec) PPM PPM PPM % of Span PPM Zero Gas 78 0.0 0.0 0.0 0.00% 0.1 Upscale Gas 76 5.05 5.0 4.9 -0.90% 5.0 System Calibration BiaS - [(System Cal. Response - Analyzer Cal. Response) 

# I Span] x 100 Drift 

# =[(Final System Cal. Response - Initial System Cal Response) 

# I Span] x 100 1114 System Cal Cal. Bias % of Span

1.12% 0.22% 

## CO 2 

## Drift, Percent of

span 1.12% 1.12%

# BARR Engineering Company EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mitlal7-day Nox CEMS Furnace Scrubber Stack A-D 3/12/08 P. Rossmiller Cylinder Serial No. Certified Value Zero Gas CC176437 0.0 

# Low-rance

Mid-ranoe CC62111 5.05 

# Hloh-ranue CC106732 8.9
ANALYZER CALIBRATION DATA Note: Difference must be less than +/- 2 percent of span Stack A - NOx(1) Analyzer Analyzer Mod / SN Model 200 Absolute Difference as Cylinder Value Calibration Difference % of Span Analyzer Span: 8.9 Response Zero Gas 0.0 0.0 0.0 0.00% Low- 

# Ranqe 0 0.0 0.00% Mid - Range 5.05 5.0 0.1 0.79% High - Range 8.9 8.9 0.0 0.22% SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed +/- 5 percent of span. Drift cannot exceed +/- 7.5 percent of span
Cylinder Value

CO 2 

## Drift, Percent of 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-range HiQh-range Mitlal7-day Nox CEMS Furnace Scrubber Stack A-D 3/12/08 

# P. Rossmiller Cylinder Serial No. CC176437 CC62111 CC106732
ANALYZER CALIBRATION DATA Certified Value 0.0 5.05 8.9

Note: Difference must be less than 

# +1- 2 percent of span Stack A - NOx(1) Analyzer Analyzer Mod 

# 1 SN Model 200 Cylinder Value Calibration Analyzer Span: 8.9 Response Zero Gas 0.0 0.0 Low- Range 0 Mid - Range 5.05 5.0 High - Range 8.9 8.9 Absolute Difference 0.0 0.0 0.1 0.0 

# EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span Difference as % of Span

0.00% 0.00% 0.79% 0.22% Initial Values Final Values 3/13/2008 

# 1114 3/14/2008 

# Cylinder Analyzer Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, STACK A (1) Time (sec) PPM PPM PPM % of Span PPM Zero Gas 78 0.0 0.0 0.1 1,12% 0.0 Upscale Gas 76 5.05 5.0 5.0 0.22% 4.9



# - System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span] x 100 Drift 

# = [(Final System Cal. Response -Initial System Cal Response) 

# 1 Span] x 100 739 System Cal Cal. Bias % of Span

0.00% -0.90% CO 2 

# Drift, Percent of

span -1.12% -1.12%

# BARR Engineering Company EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Millal 7-day Nox CEMS Furnace Scrubber Stack A-D 3/12/08 P. Rossmiller Cvlinder Serial No. Certified Value Zero Gas CC176437 0.0 low-ranoe

Mid-ranae CC62111 5.05 HTcih-ralloe CC106732 8.9
ANALYZER CALIBRATION DATA Note: Difference must be less than 

# +/- 2 percent of span SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +/- 5 percent of span. Drift cannot exceed 

# +/- 7.5 percent of span



# CO 2 

# System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) / Span] x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) / Span] x 100 Initial Values Final Values 3/13/2008 739 3/14/2008 2151 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK A (1) Time (sec) PPM PPM PPM % of Soan PPM % of Soan soan Zero Gas 78 '0.0 0.0 0.0 '0'00% 0.0 

# iO.OOo/J' 

# TO'oo% Upscale Gas 

# 76 /5,05. 4.9 5,0 ·.0.22°;" 

# Ty T120/0



# - Stack A - NOx(1) Analyzer Analyzer Mod / SN Model 200 Cylinder Value Calibration Absolute Difference as Analyzer Span: 8.9 Response Difference % of Span Zero Gas 0.0 0,0 0.0 0,00% low- Ranoe 0 0.0 0,00% Mid - Range 5,05 5.0 0.1 0.79% High - Range 8,9 8.9 0.0 0.22% 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas low-range

Mid-range High-range Mittal 7-day Nox CEMS Furnace Scrubber Stack A-D 3/12/08 

# P. Rossmiller Cylinder Serial No. CC176437 CC62111 CC106732
ANALYZER CALIBRATION DATA Certified Value 0.0 5.05 8.9

Note: Difference must be less than 

# +/- 2 percent of span Stack A - NOx(1) Analyzer Analyzer Mod 

# 1 SN Model 200 Cylinder Value Calibration Analyzer Span: 8.9 Response Zero Gas 0.0 0.0 low- RanQe 0 Mid - Range 5.05 5.0 High - Range 8.9 8.9 Absolute Difference 0.0 0.0 0.1 0.0 

# EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed 

# +/- 5 percent of span. Drift cannot exceed 

# +/- 7.5 percent of span Difference as % of Span

0.00% 0.00% 0.79% 0.22% Initial Values Final Values 3/13/2008 

# 739 3/14/2008 

# Cylinder Analyzer Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, STACK A (1) Time (sec) PPM PPM PPM % of Span PPM Zero Gas 78 0.0 0.0 0.0 0.00% 0.0 Upscale Gas 76 5.05 5.0 4.9 -0.90% 5.0



# - System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span] x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) 

# 1 Span] x 100 2151 System Cal Cal. Bias % of Span

0.00% 0.22% 

# CO 2 

# Drift, Percent of

span 0.00% 1.12%

# BARR Engineering Company 

# EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mitlal7-day Nox CEMS Furnace Scrubber Stack A-D 3/16/08

AGA Cvlinder Serial No. Certified Value Zero Gas CC176437 0.0 Low-rance

Mid-ranqe CC62111 5.05 Hloh-ranoe 

# CC106732 8.9
ANALYZER CALIBRATION DATA Note: Difference must be less than +/- 

# 2 percent of span SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed +/- 

# 5 percent of span. Drift cannot exceed +/- 

# 7.5 percent of span

CO 2 

# System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) / Span) x 100 Drift 

# = [(Final System Cal. Response -Initial System Cal Response) / Span) x 100 Initial Values Final Values 3/16/2008 2130 ·3/17/2008 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK A (1) Time (sec) PPM PPM PPM 

# % of Span PPM 

# % of Soan span Zero Gas 78 .0.0 '·0.0 0.0 ·0.000/0 0.0 :":0.00% :.:0:00% Upscale Gas 76 5:05 

# ·i 

# <5:0 ::i. 4.9 -1:120/0: 4.9 "1.12%' Q.oO%



# - Difference as



# % of Span Absolute Difference Analyzer Calibration Response Cylinder Value

Mid - Range Zero Gas Low- Ran e High - Range Stack A - NOx(1) Analyzer Mod / SN Model 200 Analyzer Span: 8.9 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-ran!:Je Hiqil-ranqe Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/16/08 

# AGA Cylinder Serial No. CC176437 CC62111 CC106732
ANALYZER CALIBRATION DATA Certified Value 0.0 5.05 8.9

Note: Difference must be less than +/- 

# 2 percent of span Stack A - NOx(1) Analyzer Analyzer Mod 

# 1 SN Model 200 Cylinder Value Calibration Analyzer Span: 8.9 Response Zero Gas 0.0 0.0 Low- Range 0 Mid - Range 5.05 5.0 High - Range 8.9 9.0 Absolute Difference 0.0 0.0 0.0 0.1 

# EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed +/- 

# 5 percent of span. Drift cannot exceed +/- 

# 7.5 percent of span
Difference as

% of Span

0.00% 0.00% 0.56% 1.12% Initial Values Final Values 3/16/2008 

# 2130 3/17/2008 

# Cylinder Analyzer Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, STACK A (1) Time (sec) PPM PPM PPM % of Span PPM Zero Gas 78 0.0 0.0 0.0 0.00% 0.0 Upscale Gas 76 5.05 

# . 5.0 4.9 -1.12% 4.9



# - System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# I Span) x 100 Drift 

# = [(Final System Cal. Response -Initial System Cal Response) 

# 1 Span] x 100 System Cal Cal. Bias % of Span

0.00% -1.12% CO 2 

# Drift, Percent of

span 0.00% 0.00%

# BARR Engineering Company EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION Project Sample loco Date Operators Miltal7-day Nox CEMS Furnace Scrubber Stack A-D 

# 3/16/08 AGA

Initial Values Final Values 3/17/2008 941 

# 3/18/2008 828 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK A (1) 

# Time (sec) PPM PPM PPM % of Soan PPM % of Soan soan Zero Gas 78 0.0 0.0' 0.0 

# .'**().()Oo/~** 0.0 

# O.()O% 0.00% Upscale Gas 76 5.05' (;'0 

# .,f 4.9 

# ,t11.12% 4.8 "2:25% 

# \t1.12°/o Cvlinder Serial No. Certified Value Zero Gas CC176437 0.0 Low-rance

Mid-ranQe CC62111 5.05 

# Hiqh-ranqe CC106732 8.9
ANALYZER CALIBRATION DATA Note: Difference must be less than 

# +1-2 percent of span Stack A - NOx(1) Analyzer Analyzer Mod 

# 1 SN Model 200 Cylinder Value Calibration Absolute Difference as Analyzer Span: 8.9 Response Difference % of Span Zero Gas 0.0 0.0 0.0 0.00% low- Rance 0 0.0 0.00% Mid - Range 5.05 5.0 0.0 0.56% High - Range 8.9 9.0 0.1 1.12% SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +1-5 percent of span. Drift cannot exceed +/- 

# 7.5 percent of span

System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span] x 100 Drift 

# =[(Final System Cal. Response - Initial System Cal Response) / Span] x 100 CO 2 

# BARR Engineering Company Project Sample loco Date Operators

Zero Gas low-range

Mid-range High-range Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/16/08 AGA Cylinder Serial No. CC176437 CC62111 CC106732
ANALYZER CALIBRATION DATA Certified Value 0.0 5.05 8.9

Note: Difference must be less than +/- 

# 2 percent of span Stack A - NOx(1) Analyzer Analyzer Mod / SN Model 200 Cylinder Value Calibration Analyzer Span: 8.9 Response Zero Gas 0.0 0.0 low- RanQe 0 Mid - Range 5.05 5.0 High - Range 8.9 9.0 Absolute Difference 0.0 0.0 0.0 0.1 

# EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed +/- 

# 5 percent of span. Drift cannot exceed +/- 

# 7.5 percent of span Difference as % of Span

0.00% 0.00% 0.56% 1.12% Initial Values Final Values 3/17/2008 941 3/18/2008 Cylinder Analyzer Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, STACK A (1) Time (sec) PPM PPM PPM % of Span PPM Zero Gas 78 0.0 0.0 0.0 0.00% 0.0 Upscale Gas 76 5.05 5.0 

# 4.9 -1.12% 4.8 System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) / Span] x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) / Span] x 100 828 System Cal Cal. Bias % of Span

0.00% -2.25% CO 2 

# Drift, Percent of

span 0.00% -1.12%

# BARR Engineering Company EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Mitlal7-day Nox CEMS Furnace Scrubber Stack A-D 3/18/08 AGA Cylinder Serial No. Certified Value Zero Gas CC176437 0.0 Low-rance

Mid-ranee CC62111 5.05 Hiqh-ranqe CC106732 8.9
ANALYZER CALIBRATION DATA Note: Difference must be less than 

# +/- 2 percent of span Stack A - NOx(1) Analyzer Analyzer Mod / SN Model 200 Cylinder Value Calibration Absolute Difference as Analyzer Span: 8.9 Response Difference % of Span Zero Gas 0.0 0.0 0,0 0.00% Low- Rance 0

# ~+- 0.00% . Mid - Range 5.05 5.0 1.12% . High - Range 8.9 9.0 0,1 

# I 0.90% SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +/- 5 percent of span. Drift cannot exceed 

# +/- 7.5 percent of span Initial Values Final Values 3/18/2008 936 3/19/2008 756 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK A (1) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 78 0,6 0.0 0.0 .0.00"10. 0,0 .0.000/. >0.000/.( Upscale Gas 76
. 

## 5,05 5.b**4~9** 

## "cb,56% '5.0 0.56% 1.12% System Calibration Bias 

# = [(System Cal. Response - Analyzer Cal. Response) / Span) x 100 Drift 

# =[(Final System Cal. Response -Initial System Cal Response) / Span) x 100 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-range High-range Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 

# 3/18/08 AGA Cylinder Serial No. CC176437 CC62111 CC106732
ANALYZER CALIBRATION DATA Certified Value 0.0 5.05 8.9

Note: Difference must be less than 

# +/- 2 percent of span "'I 0/. 

## uuc 

# Stack A - NOx(l) Analyzer Analyzer Mod / SN Model 200 Cylinder Value Calibration Analyzer Span: 8.9 Response Zero Gas 0.0 0.0 Low- Range 0 Mid - Range 5.05 5.0 High - Range 8.9 9.0 Absolute Difference 0.0 0.0 0.1 0.1 

# EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed 

# +/- 5 percent of span. Drift cannot exceed 

# +/- 7.5 percent of span
Difference as

% of Span

0.00% 0.00% 1.12% 0.90% Initial Values Final Values 

# 3/18/2008 936 

# 3/19/2008 Cylinder Analyzer Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, STACK A (1) Time (sec) PPM PPM PPM % of Span PPM Zero Gas 78 0.0 0.0 0.0 0.00% 0.0 Upscale Gas 76 5.05 5.0 4.9 -0.56% 5.0 System Calibration Bias 

# = [(System Cal. Response - Analyzer Cal. Response) / Span) x 100 Drift 

# = [(Final System Cal. Response -Initial System Cal Response) / Span) x 100 756 System Cal Cal. Bias % of Span

0.00% 0.56% Drift, Percent of

span 0.00% 1.12%

# BARR Engineering Company EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION Project Sample Lac. Date Operators Miltal 7-day Nox CEMS Furnace Scrubber Stack A-D 3/18/08 

# AGA Cvlinder Serial No. Certified Value Zero Gas CC176437 0.0 Low-ranee

Mid-ranee CC62111 5.05 High-range CC106732 8.9 ANALYZER CALIBRATION DATA Note: Difference must be less than 

# +1- 2 percent of s an SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span

CO 2 

# System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span) x 100 Drift 

# =[(Final System Cal. Response -Initial System Cal Response) 

# 1 Span] x 100 Initial Values Final Values 3/18/2008 

# 936 3/19/2008 

# 756 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK A (1) Time (sec) PPM PPM PPM 

# % of Span PPM 

# % of Span span Zero Gas 78 

# lJ.O i 0.0 0.0 

# O.lJO% 0.0 

# lJ.lJlJ"Ici ilJ;oo%1. Upscale Gas 76 5.05 5.0 4.9 -0.56% 5.0 i 0.56"1oi 

# 1'.12%



# - Absolute Difference as Difference % of Span Analyzer Calibration Response Cylinder Value
Zero Gas Mid- Range Low- Ran e High - Range Stack A - NOx(1) Analyzer Mod 1 SN Model 200 Analyzer Span: 8.9 

# BARR Engineering Company Project Sample Lac. Date Operators

Zero Gas Low-ranqe

Mid-ranqe High-range Millal 7-day Nox CEMS Furnace Scrubber Stack A-D 3/18/08 

# AGA Cylinder Serial No. CC176437 CC62111 CC106732
ANALYZER CALIBRATION DATA Certified Value 0.0 5.05 8.9

Note: Difference must be less than 

# +1- 2 percent of span oJ/IO/,<UUO 

# Stack A - NOx(1) Analyzer Analyzer Mod 

# 1 SN Model 200 Cylinder Value Calibration Analyzer Span: 8.9 Response Zero Gas 0.0 0.0 Low- Range 0 Mid- Range 5.05 5.0 High - Range 8.9 9.0 Absolute Difference 0.0 0.0 0.1 0.1 

# EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span
Difference as



# % of Span

0.00% 0.00% 1.12% 0.90% Initial Values Final Values 3/18/2008 

# 936 3/19/2008 

# Cylinder Analyzer Cal System Cal System Cal Systern Cal Response Value Response, Response, Cal. Bias Response, STACK A (1) Time (sec) PPM PPM PPM % of Span PPM Zero Gas 78 0.0 0.0 0.0 0.00% 0.0 Upscale Gas 76 5.05 5.0 4.9 -0.56% 5.0



# - System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span) x 100 Drift 

# =[(Final System Cal. Response -Initial System Cal Response) 

# 1 Span) x 100 756 System Cal Cal. Bias % of Span

0.00% 0.56% CO 2 

# Drift, Percent of

span 0.00% 1.12%

# BARR Engineering Company EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc. Date Operators Miltal7-day Nox CEMS Furnace Scrubber Stack A-D 3/20/08 AGA Cvlinder Serial No. Certified Value Zero Gas CC176437 0.0 

# Low-rance

Mid-ranQe CC62111 5.05 

# Hiqh-ranqe CC106732 8.9 ANALYZER CALIBRATION DATA Note: Difference must be less than 

# +/- 2 percent of s an SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +/- 5 percent of span. Drift cannot exceed 

# +/- 7.5 percent of span

System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) / Span] x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) / Span] x 100 Initial Values Final Values 3/19/2008 756 3/20/2008 754 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response, Cal. Bias Percent of STACK A (1) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 78 

# O.() 0.0 0.0

# <()~ •• 0.1 1.1:2% 1.12% Upscale Gas 76 ·.. 5.05 5.0 5.0 

# .0;:
. 5.1 1.24% 0.67%



# - Difference as

% of Span Absolute Difference

9.0 5.0 0.0 Analyzer Calibration Response Cylinder Value

Mid - Range Zero Gas Low- Ran e High - Range Stack A - NOx(1) Analyzer Mod / SN Model 200 Analyzer Span: 8.9 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-range High-range Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 

# 3/20/08 AGA Cylinder Serial No. CC176437 CC62111 CC106732
ANALYZER CALIBRATION DATA Certified Value 0.0 5.05 8.9

Note: Difference must be less than 

# +1- 2 percent of span ;)IIO/LUUC 

# Stack A - NOx(1) Analyzer Analyzer Mod 

# 1 SN Model 200 Cylinder Value Calibration Analyzer Span: 8.9 Response Zero Gas 0.0 0.0 Low- Range 0 Mid - Range 5.05 5.0 High - Range 8.9 9.0 Absolute Difference 0.0 0.0 0.1 0.1 

# EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span Difference as

% of Span

0.00% 0.00% 1.12% 0.90% Initial Values Final Values 

# 3/19/2008 756 

# 3/20/2008 Cylinder Analyzer Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response, STACK A (1) Time (sec) PPM PPM PPM % of Span PPM Zero Gas 78 0.0 0.0 0.0 0.00% 0.1 Upscale Gas 76 5.05 5.0 5.0 0.56% 5.1



# - System Calibration Bias - [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span] x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) 

# 1 Span] x 100 754 System Cal Cal. Bias % of Span

1.12% 1.24% Drift, Percent of

span 1.12% 0.67%

# BARR Engineering Company EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc, Date Operators Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 3/20/08 AGA Cvlinder Serial No, Certified Value Zero Gas CC176437 0,0 Low-rance

Mid-range CC62111 5.05 Hiah-ranae CC106732 8.9

CO 2 

# SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed +/- 

# 5 percent of span. Drift cannot exceed +/- 

# 7.5 percent of span

System Calibralion Bias 

# = [(System Cal. Response - Analyzer Cal. Response) / Span] x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) / Span] x 100 Initial Values Final Values 3/20/2008 754 3/21/2008 841 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift, Response Value Response, Response, Cal. Bias Response. Cal. Bias Percent of STACK A (1) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 78 

# 1>'0 

# i>.o 0.1 

# r.
0.0 .··lJ;lJO% "1;12°10 Upscale Gas 76 >5.05 •• 5.0 5.1 5.0 0.56% -0.67% 

# t 

# f ANALYZER CALIBRATION DATA N t D'ff t b I th / 2

o e: I 

# erence mus e ess an 

# +- percen 0 

# span Stack A - NOx(1) Analyzer Analyzer Mod / SN Model 200 Absolute Difference as Cylinder Value Calibration Difference % of Span Analyzer Span: 8,9 Response Zero Gas 0.0 0.0 0.0 0.00% Low- Rance 0 0.0 0.00% Mid - Range 5.05 5.0 0.1 1.12% High - Range 8.9 9.0 0.1 0.90% 

# BARR Engineering Company Project Sample Loc. Date Operators

Zero Gas Low-range

Mid-range Hiqh-ranqe Mittal7-day Nox CEMS Furnace Scrubber Stack A-D 

# 3/20/08 AGA Cylinder Serial No. CC176437 CC62111 CC106732
ANALYZER CALIBRATION DATA Certified Value 0.0 5.05 8.9

N t D'ff tb I th

o e: I 

# erence mus e ess 1 2 an 

# +- t 

# f percen 0 

# span Stack A - NOx(1) Analyzer Analyzer Mod 

# 1 SN Model 200 Cylinder Value Calibration Analyzer Span: 8.9 Response Zero Gas 0.0 0.0 Low- Range 0 Mid - Range 5.05· 5.0 High - Range 8.9 9.0 Absolute Difference 0.0 0.0 0.1 0.1 

# EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA:

Note: System Cal bias cannot exceed +1- 5 percent of span. Drift cannot exceed +1- 7.5 percent of span Difference as % of Span

0.00% 0.00% 1.12% 0.90% Initial Values Final Values 

# 3/20/2008 754 

# 3/21/2008 Cylinder Analyzer Cal System Cal System Cal System Cal Response Value Response, Response, Cal. Bias Response. STACK A (1) Time (sec) PPM PPM PPM % of Span PPM Zero Gas 78 0.0 0.0 0.1 1.12% 0.0 Upscale Gas 76 5.05 5.0 5.1 1.24% 5.0 System Calibration Bias 

# = [(System Cal. Response - Analyzer Cal. Response) 

# 1 Span] x 100 Drift 

# = [(Final System Cal. Response - Initial System Cal Response) 

# 1 Span] x 100 841 System Cal Cal. Bias % of Span

0.00% 0.56% CO 2 

# Drift, Percent of

span -1.12% -0.67%

# BARR Engineering Company EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION Project Sample Loc, Date Operators Mitlal7-day Nox CEMS Furnace Scrubber Stack A-D 3/20/08 AGA Cvlinder Serial No, Certified Value Zero Gas CC176437 0.0 low-range

Mid-ranee CC62111 5.05 High-range CC.106732 8.9
SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +/- 5 percent of span, Drift cannot exceed 

# +/- 7.5 percent of span

System Calibration Bias 

# = [(System Cal. Response - Analyzer Cal. Response) / Span] x 100 Drift 

# =[(Final System Cal. Response - Initial System Cal Response) / Span] x 100 Initial Values Final Values 3/21/2008 841 3/22/2008 754 Cylinder Analyzer Cal System Cal System Cal System Cal System Cal Drift. Response Value Response. Response. Cal. Bias Response. Cal. Bias Percent of STACK A (1) Time (sec) PPM PPM PPM % of Span PPM % of Span span Zero Gas 78 <0.0 

# 'i,i 

# ll.ll 0.0 (J,oOo/d 0.0 • (J.(JO%

# '(J~6(J% Upscale Gas 76 ·5,(J5 5:0 5.0 '0.56%'::< 5.(J .(J,56% (J,OO% ANALYZER CALIBRATION DATA 

# N 

# t D'ff b h

oe: I 

# erence must e less t an 

# + - 2 percent 0 

# span Stack A - NOx(1) Analyzer Analyzer Mod 

# I SN Model 200 Cylinder Value Calibration Absolute Difference as Analyzer Span: 8,9 Response Difference % of Span Zero Gas 0.0 0.0 0.0 0.00% low- Range 0 0.0 0.00% Mid - Range 5.05 5.0 0.1 1.12% High - Range 8.9 9.0 0,1 0.90% 

# BARR Engineering Company Project Sample loco Date Operators

Zero Gas low-range

Mid-range High-range Mittal7-day Nox CEMS Fumace Scrubber Stack A-D 

# 3/20/08 AGA Cylinder Serial No. CC176437 CC62111 CC106732
ANALYZER CALIBRATION DATA Certified Value 0.0 5.05 8.9



# N 

# t D'ff b h

oe: I 

# erence must e less t an 

# + - 2 percent 0 

# span vIIOI<;UUO 

# Stack A - NOx(1) Analyzer Analyzer Mod 

# I SN Model 200 Cylinder Value Calibration Analyzer Span: 8.9 Response Zero Gas 0.0 0.0 low- Range 0 Mid - Range 5.05 5.0 High - Range 8.9 9.0 Absolute Difference 0.0 0.0 0.1 0.1 

# EPA METHOD 3A CO 2 

# CEMS ANALYZER CALIBRATION

SYSTEM CALIBRATION BIAS AND DRIFT DATA: Note: System Cal bias cannot exceed 

# +1- 5 percent of span. Drift cannot exceed 

# +1- 7.5 percent of span Difference as

% of Span

0.00% 0.00% 1.12% 0.90% Initial Values Final Values 

# 3/21/2008 841 

# 3/22/2008 Cylinder Analyzer Cal System Cal System Cal System Cal Response Value Response. Response. Cal. Bias Response. STACK A (1) Time (sec) PPM PPM PPM % of Span PPM Zero Gas 78 0.0 0.0 0.0 0.00% 0.0 Upscale Gas 76 5.05 5.0 5.0 0.56% 5.0 System Calibration Bias 

# = [(System Cal. Response - Analyzer Cal. Response) I Span] x 100 Drift 

# =[(Final System Cal. Response - Initial System Cal Response) I Span] x 100 754 System Cal Cal. Bias % of Span

0.00% 0.56% Drift. Percent of

span 0.00% 0.00%

# Appendix C Instrument Output 

# Appendix C Instrument OutputRece-ded Data**15-rr ~u** **te av** **:a., ws** 



# , STACK A- 

### inputs STACK B - 

### inputs STACK 

### c-f nputs STACK 

## D- inputs TOAS NOx CE MS CR101.."'(l 

### 4789 :',OOO .$(Ij C8 Tat : e ' S T IMESTA,'lP RECORD ;uPr cs.::U"HTmp _F_Al5b l : P

_A vp 02-Avg(l**02.-Avg ( 1 )** **Avg .irF1owl** **Yl: p_**  _A
.... >02 _Ayg(l 02_A' ...g(2p Y.2_Avg (2.irF'low2.-Av.TmpJ_A ygl yg 

### mp -**A"" 9(** **02_Avg (4)~_A** **vg (4.irAow4_AdcTmp_F**  _A
.... g (4) TS 

### RN 

# ..... D", F n H20 

### ppmO<y P rcnt Dry P cntOry 

### Wi20 

### D
.. F ppmD" Prcn tOry**~cntOry** nH 20 

### DogF 

# T "'"'lliy OoOF ppm"'" PrcntDry Pent"'" 

### " H2O D<gF 

# '" A yg A \'9 A yg Ayg Ayg A yg Ayg Ayg A"" A"" A • • A"" A Ayg Ayg A • • Av. Ayg 28: 25 4 

### :0.14 3
. 1 1 8
. 6 

### 1 .2 0 .6 "0 3 

### 19.3 1.2 Q 18.B 1.7 18 .0 

### 2A 1 .23 4 31 28. 25 23 -0.14 3. 4 1 9.0 1.2 0
. '" 11 0 25 

### 19 .3 1.2 0.62 110 Inv <Uddata 

### '8 .6 1.7 0 .85 117 2 .6 78.0 Z4 12' 32 28.z,: 23 -0. ' 4 35 19.2 1.2 0
. 06 1 11 2 .5 

### 1 9.3 1 .2 0 .91 110 l n vaid dab. 

### 18 .6 1.7 0 .84 117 V 18.0 2 .4 ' 24 

### 33 23.23 22 -0
. ' 4 2' 19.2 '3 0
. '" 

### u t 2 .2 

### 19.3 1.2 0.92 110 I nva id data 

### 1 8.6 1.7 063 117 26 18.0 2.4 12.; 34 23.23 2 ' -0.1 4 2.6 19.2 13 0.90 " 0 2.0 

### 19.3 1.2 0.93 '09 Invakl data 18.6 1.7 084 " 6 26 18.0 2.4 124 35 2822 2 ' -0. 14 2.3 19.2 13 0.91 

# 10' 1. 6 

### 19.3 1.2 0.95 

### tc 1 nV3id Ijala 

### 78 .6 1.7 0.86 11 6 26 18.0 Z4 123 36 28.2' 2' -0. 14 2. 4 19.2 1.2 0.902 

### rca 1., 

### 19.3 1.2 0.97 

# '08 Invat'd da13. 18.B 1.7 0.8 5 " 5 25 18.0 

### 2A ' 23 3 7 2820 21 

### ·0
. 14 3.2 19.2 1.2 0 .89 " 0 2 .4 

### '9 .3 1.2 0.96 

# '09 Invai d da ta 

### 18.6 1.7 0.84 " 6 2.5 18.0 2.4 ' 23 3B 29
. '9 20 · 0. 1 4 3.0 19 .2 1.2 0. 69 " 0 24 

### '9 .3 1.2 0 .95 

### tc Invaiijdala 

### 18.6 1.7 0.84 116 2.6 18.0 2.4 '23 3' 28
. '8 21 · 0.15 3.6 19 .2 12 0.89 " 0 2.7 

### '9 .3 1.2 0. 95 

## tc**da1a** 

### 18 .6 1.7 0 .64 "6 2.6 18.0 Z4 1 23 

# "'" 28
. '7 20 -0
. 14 27 19.2 12 0.91 

# r c 2.2 

### 19 .3 1.2 0. 95 

## ic 

# """"' - 18 .6 1.7 0 .00 " 6 2.3 18.0 Z4 1 23 4\ 26
. '7 21 -0
. 15 3. 1 19 ,2 1.2 0.91 

## rc 24 

### 19 .3 1.2 0 ,97 

## ic 

# """"" - 18.B 1.7 0 .65 11 6 2 .3 18.0 

### 2A ' 23 42 28 .16 20 -0
. '5 3 .5 ' 9.2 12 0.9' 

# '" 27 

### 19 .3 1.2 0. 96 ' 0' lnval .d da l.3. 

### 18.6 ' .7 0 .85 116 2.3 18.0 2 .4 1 23 43 28
. 15 20 · 0
. 14 3 .6 192 1.2 0. 90 

### ,eg 2' 

### '9 .3 1.2 0. 96 ' 09 Invaid da la 

### 18.6 • .7 065 

## u e 2 .4 '8.0 

### 2A 1 22 44 28
. 14 20 · 0 .1 4 3. 7 1 9.2 1.2 0 .92 "0 27 

### ' 9.3 1.2 0 .96 109 Jnva! id dal a 

### 18.6 1.7 0.65 116 24 18.0 2 .4 ' 23 45 28 .13 20 .Q
. 14 3.6 19. 2 1 .2 0 .90 IC' 26 

### '9 .3 1.2 0.96 109 

# """"' - 1 8.6 '.7 0 .65 

## us 23 '8.0 2 .4 ' 23 

### 46 28
. 12 

### 20 .0
. 1 4 4.0 19.2 1 .2 0 90 109 3 .0 

### '9 .3 1.2 0 .94 109 Invalid data 

### 18.6 1.7 000 

## us 2. 4 18 .0 2 .4 123 47 28
. 1 1 

### 20 .0
. 14 4
. 1 1 9 .1 1
.2 0
. 9 1 110 31 

### 1S .3 12 0
. 95 .09 Inva/id lhfa 

### 18.6 •.7 0. 64 "6 2... 18.0 Z4 

### '23 48 28
. 1 1 20)
· 0. 1 4 3. 7 19 .1 1
.2 0
. 9 1 109 29 

### 19 .3 1.2 0
.94 109 

# ' '''''''' 

# .... 18.8 

## t. r 0. 65 1t6 23 '8 .0 2 .4 123 49 28.1 0 21 .0
. 1 4 35 19. 2 1
.2 0
. 92 . 09 28 

### 19 .3 1.2 0
. !i05 109 I m aid data 

### 1 8.6 ' .7 0 .86 1t 6 24 18 .0 2 .4 123 50 28
. 10 21 .0
. 1 4 4 0 1 9 .1 1
. 2 0
. 9 1 109 32 

### 19 ,3 1.2 0
.97 109 I m aid data 

### 1 8.6 '. 7 0 .86 1t 6 Z 4 18.0 2 .4 123 51 2866 21 .0
. 1 4 .. .5 1 9.1 1
.2 0 ,9 1 11 0 3 4 

### 19 .3 1.2 0
.94 109 I m aid data 

### 1 8.6 ' .7 O .s.; 116 2S 1 8.0 2 .4 123 52 2866 

### 21 -0 .14 3 .8 1 9.1 1
.2 0 .90 109 3 0 

### 19 ,3 12 0
.94 109 

### I nvaXI d.11a 

### ' 8.8 ' .7 0 85 1t 6 24 78.0 2 .4 123 53 28 .07 22 -0 .1 4 4 .2 19.1 '2 0 .92 11 0 3 .3 

### IS.3 1.2 0. 93 11 0 l nvaid d3Ia
. 8.B t.7 0
. 85 117 24 18.0 2 .4 123 54 2805 

### 21 ·01 4 4 .5 1 9.1 '. 2 090 11 0 3 .7 

### 1 9 .3 1.2 

### o.s- 11 0 Invaid data 18.B 1.7 0. 00 117 2 .3 18.0 2 .4 123 55 28.05 

### 20 -0
. 1 4 36 1 9.1 ' .2 0.91 110 3 0 

### /S.3 

### 1.2 0.'" '09 I nvatd da ta 

### 78 .6 1.7 0. 85 11 0 2.3 1 8.0 2 .4 1 23 56 23.04 

### 20 -0
. '" 3.7 1 9.1 ' .2 090 109 3 0 

### 19 .3 1.2 0.'" '09 I nvaid data 18.6 1.7 0
. 87 "6 23 18.0 Z4 122 57 28 .03 20**-o.I~** 44 1 9.1 '2 0.90 " 0 

### 35 19.3 1.2 0. '" 109 lrwaid**d~a** 

### 18.6 1.7 0.66 "6 24 18 .0 

### 2A 123 58 28.03 20 -0
. 14 4 .4 19 .1 1.2 0 .92 "0 3 .5 

### 19 .3 1.2 0.S 3 10' Invaid d<lU 

### 18 .6 1.7 0
. 65 115 2.3 1 8.0 Z4 122 59 2a ,03 19 

### -0 .14 4 ,9 19.2 '2 0 .91 110 40 

### '9 .3 1.2 0.9 3 '09**I~data** 

### 1 8.6 •.7 0 .85 116 2.5 18.0 2 .4 122 60 28.02 19 

# -c.r a 4 .7 19.1 1.2 0. 91 ,, 0 

### J.7 19 .3 1.2 0. 93 10' I nv aid data 

### 18 .6 1.7 0 .66 

### '15 2 .5 18.0 Z4 '22 6' 28.02 19 -0
. 14 4.7 19.2 1.2 o , £OJ 11 0 3 .7 

### 19 .3 1.2 0.87 109 Inv aid data 

### ' 8.6 

# '.7 0 .85 1 15 2S 18.0 Z4 '22 62 28.02 19 -0. 14 5. 2 19.1 '2 0.91 111 4
. ' 

### 19.3 1.2 0.82 100 Invalid data 18.B 1.7 0 .66 11 6 2.S 18.0 2 .4 122 53 28 .02 19 -0.1 4 5. 1 19,1 '2 0.00 110 4 .' 

### '9 .3 1.2 0,82 

## tc I nvaid da ta 

### '8 .6 1.7 0.66 11 6 2.5 18.0 Z4 '23 64 28.0 1 19 · 0. 14 4.4 19.1 1.2 0.89 " 0 3 .6 

### '9 .3 1.2 0.90 

### ,C3 Invaid datil 

### 18 .6 1.7 085 115 23 18.0 

### 2A ' 22 6 5 28.0 1 '6 -0 .1 4 4 .6 '9.1 12 0 .90 

# ", 3 .6 

### '9 .3 1.2 0.96 

### ,C3 In vaJ,

ddata 

### 18.6 •.7 0.66 " 6 2.4 18.0 2.4 '23 66 2a .0 1 1 6 -0
. 14 4 .6 1 9.1 1.2 0. 69 " 0 3 .6 

### 19.3 1.2 I.OJ 

## ic Wlvaidda la 

### 18.6 1,7 

### 0.85 1 16 2.3 /8.0 

### 2A 1 23 67 23 .00 19 -0.1 4 4 .' 19 .1 '2 0.9 1 111 4
.0 

### '9.3 1.2 1.OJ 

### ,C3 Inva6id da ta 

### 18.6 1,7 0.85 11 6 2.3 18.0 

### 2A ' 23 66 28 .00 20 · 0 .14 5.3 1 9.1 1.2 0.88 

# ", 42 '9 .3 1.2 1.02 ,C9 mat:d 

### dat a 18.B 

# t.r 0 .85 " 6 23 18.0 

### 2A 123 6' 2800 20 .{)
. 1 3 5.3 '9. 1 1.2 0.90 

# ' " 43 '9 .3 1 .2 1.OJ 'C' Invalld d a.ul 

### 18.6 1.7 

### 0
.82 116 2.4 18.0 2.4 123 70 2800 

### 21 .{)
. 13 4
.7 1 1U 1
.2 0. 90 11. 36 

### '9 .3 1.2 0. 99 

## ic lnv*j dal a 

### 18.6 '. 7 

### 0 .8 1 11 6 2 .2 '8.0 

### 2A 1 23 7
. 28 .00 22 .{)
. 1 3 2 .7 6 . ' 0. 6 0 .90 111 3 

## .e 19.3 1.2 0.66 ItO V1vaIidda ta 

### 18 .6 ' .7 

### 0
. 79 117 2 .' 18.0 2.4 124 Stac k A

- System 

### Bias Check 72 28 .0 1 22 .{)
. 1 3 2 .6 1 1 .2 3.0 0.69 112 3 .5 

### 19 .3 1.2 0 .99 110 InvaIid dal a 

### 18.6 1.7 0
.77 " 6 20 18.0 2.4 124 Stack A

- System Bias Check 73 23.00 23 .{)
. 1 3 26 1 6 .0 

# ae 0
. 00 11 1 2 ' 

### '9 .3 1 .2 1
.00 It O 

### Inv alid data 

### 18.6 t.7 0 .65 11 7 2 ' 18 .0 

### 2A 0. 18 124 3 - S y s tem 

### BiasChock I Stack 0 /llJ r Flow S«lsor' 74 26 .t>J 23 .0
. 12 5.0 19 .4 1
.2 0 ,89 111 55 

### '9 .3 1.2 1 .2 4 110 I n'' J <J: id data 1B .6 •.7 0
.70 117 2 ' 18 .0 2 .4 

# ""
.50 '23 Stack 0 

### P¥ Row**~sor** Ott-Wie 75 28 .00 2 3 · 0
. 1 2 5 .5 19
. 5 1.1 090 111 45 

### '9 .3 1.2 1
. 01 109 

# """"" - 1B .6 t.7 080 116 1
. ' 

### 18.0 Z4 

# "".50 122 : - SY10lern 

### BiasCheck I Stac k 0 M 

### Flow

## s.nsor . 76 28 .00 23 .0
. 12 6 .6 19.5 1
. 1 0 .88 112 

### 55 'S .3 1.2 0 .79 110 Inv a ld data 

### 1 8.6 •.7 0
. 62 116 5.0 

### 18 .0 2 .4 

### -O.SO 1 22 ) - Syt, lem 

### Check I Stac k 0 All 

### Flow S«lsor' 

# rr 28 .02 24 .0 .1 3 6.5 1 9
.4 1.2 0
. 87 113 5
.4 

### 19.3 1.2 0 .6 7 110 I nv<Udda ta 

### 1 8.6 • .7 060 1t7 2.6 18 .0 2 .4 

# "" .50 1 23 

### St&ck 0 

### Air

### Flow S«lSOf OO.w 76 28 .0 1 28 -0
. 14 54 1 9
.4 1.2 0. 89 111 4 5 

### I S.3 ' .2 0
. 69 110 :nvalid d31a 

### 18.6 '.7 0
. 79 1t 7 23 16 .0 2 .4 

# ""
.50 123 

### Stade: 

### 0 hr 

### FlowSiosar Oft-k'! e 7' 28 .02 

### 2.5 -0
. 14 6 1 1 9
. 5 1.1 0
.9 1 11 0 5
. 1 

### 1 9.3 ' .2 0. 9 1 11 0 l nva'icl da1a 1 8.B 1.7 0. 62 1t6 Z5 18.0 2 .4 122 60 28 .02 2 5 -0
. 1 4 7 .0 1 9
. 5 1. 1 0 .S2 11 0 6 .0 

### 19.3 1.2 0
.S 3 110 

# , """"' 

# .... .8. B 1.7 0
. 82 11 6 Z' IB .O 2 .4 122 8' 2:8.02 26 · 0. 1 3 7 .' 1 9. 6 1
.0 0 .93 11 ' 6 .5 

### 'S.3 1.2 1.OJ 110 I nvald 

### data
. 8.B ' .7 0 .62 11 6 3 .4 18 .0 2 .4 1 22 62 28 .02 28 .{). 12 6 .5 19.6 1.0 0.92 110 65 

### ' 9.3 1.2 1 .0 2 109 I nv<Ud<bIa 

### 18.6 ' .7 0 8 1 115 3.. 18.0 Z4 121 83 @.02 28 -0. 12 7.4 1 9.6 1.0 0.91 112 6 .6 

### 19.3 ' .2 1.03 11 0 tnvaid <i3la 

### 1 8.8 ' .7 0
.79 11 6 3.' 18.0 

### 2A 1 21 64 28 .02 31 

### · 0. 12 7.4 ' 9.6 0.9 0.9 1 116 

## e.S 

### 1 9.3 ' .2 1.e9 113 lnvaid d31a 

### 16. 6 1.7 0
. 81 

# ," 3.5 18.0 2. 4 124 65 23 .02 35 -0 .11 74 1 9.6 0. 9 0 ,91 "7 67 

### ' 9
. 3 1.2 1.11 

### ' 15 Invaid data 

### 1 8.8 1.7 0
. 79 120 37 1 8.0 2 .4 12< 86 28.02 

# '" ·0 10 7.5 19 .3 0 .' 0.9 ' "5 0 .8 

### '9 .3 1.2 11 3 Inv akl data I 8.B ' .7 0 60 1 18 42 18 .0 

### 2A 123 87 28.02 32
- J
. 10 6.7 19 .0 0.' 0.8 9 " 5 6 1 

### 19 .3 1.2 "2 Invaid da l a 

### 18.6 1.7 

## o .n 116 3.4 18 .0 2 .4 1 23 86 2802 

### 33

-0.09 6 .8 19.0 0.6 0 .92 " 4 6 .' 

### 1 9.3 1.2 110 IrrJakl dala 

### /6 .6 

# t .r 0. 60 115 5.1 '8 .0 2 .4 1 20) 8 ' 28,02 

# '" -0
. 10 6 .0 19.3 0.7 0 .91 " 4 6 , 

### 19
. 3 1.2 

# ", 

# """"' '''''' 18.6 1,7 

## o .n 11 6 4 .8 18.0 

### 2A 

### '20 90 28.03 35 -0,09**~5** 19.6 0.8 0.94 " 2 5
. 5 

### '9 .3 1.2 110 nvld<l dala 

### 18.6 1,7 0 .78 " 6 4 .4 18.0 

### 2A 120 

# " 28.03 35 -009 6 .0 19.1 0.8 0.&05 " 2 5 .6 

### 19.3 1.2 

# ", maid data 

### 18.6 1,7 0 .79 117 4 .3 18.0 2.4 12 1 

## sz 2O .OJ 36 · 0.C9 5.8 18.9 0.' 1 .00 

# ", 5 .6 

### '9 ,3 1.2 

# ", Inv alidcala 

### 18.6 1.7 

## o.n 117 3 .' 18.0 

### 2A '22 93 28.03 41 -0.03 6 .5 18.9 0.' 0 .95 

# ", 6 ' 

### '9 .3 1.2 "0 Invodid tiata 18.B 1.7 0.76 " 6 4.5 18.0 

### 2A 1 2 1 94 2a.03 

### 42

-003 6.0 18.8 0.' 0. '" 

# ", 5 .6 

### 19.3 1.2 110 Vwa1d a'ata 

### 18.6 1,7 0 .75 "6 4.2 18.0 

### 2A 120 95 28 .02 

# '" -o .C9 5.8 18.8 0.' ' .00 

# ,,, 5 4 

### '9.3 1.2 

# ", In v n

l:d o:a.m 

### 18.6 1,7 

### 0 .78 11 8 3.6 18.0 2.4 12 1 

# ss 28 .03 

### 45 -0 .09 6. ' 1 8.7 0.' 1.05 III 5 .6 

### 1 9.3 1.2 ,,1 Invat!d ci.l.l a 

### 18.6 1.7 

### 0 .7 5 117 3.6 /8.0 2.4 '22 '7 23 OJ 

## as
-0.08 5.' 18 .7 0 .' 1.02 

# " , 5 .3 

### 19.3 1.2 11' lnvalid da la 

### 18 .6 1.7 0.7 4 117 3.6 /8.0 2.4 '22 99 28 .OJ 47 -o.C9 5.' 18.5 1.0 1.02 112 

### S.: '9.3 1.2 

# '" """"' dal
. 18.6 1,7 0 .72 " 6 3 .3 18.0 

### 2A ' 23 99 2a.03 47 -o .C8 5 .9 

### 19.3 '. 3 1.02 "2 5 .4 

### 19.3 '. 2 11' lnvaIid data 

### 18 .6 1.7 

### 0
. 73 " 8 3 .4 18.0 2.4 123 

### 02lC02 It 100 2803 

# '" ""OS 6 .1 

### 19.3 1 .3 1 .03 "2 5 6 19.3 1 .2 11 '**Inv al** **da** 18.B ', 7 0 .72 117 3. 5 18.0 Z4 '22 101 28 OJ 

### 45 ·0
.08 6 .0 

### 79.3 1.3 1. 02 

# "' 5 ,3 19 .3 1.2 110 Invatid dai a 

### 18 .6 1.7 072. 117 3.3 18.0 

### 2A 1 22 10 2 2.1.02857 

### 46 -0.0 7 6 . 1 

### 19.3 1.3 1
.02 110 56 19 .3 1.2 109 I n "'*' dat a 

### 18.6 • .7 0.71 "S 3. 4 18 .0 2 .4 12 1 I OJ**03** 

# ... -0. 07 6 .5 

### 19.3 1.3 1.01 110 5 .7 1 9.3 12 110 

### Invalidd4la I8.B •.7 0.71 ,, 6 3
.4 18 .0 24 1 22

. 04 28 .02 

### 45 ·0. 07 0.4 

### 19.3 ' .3 '. 0 2 112 5 .8 1 9
. 3 1 .2 110 Il'M*i do1ta 

### '8.6 ' .7 0 .71 11 6 3.6 '8.0 

### 2A 121 105 26 .03 47 · 0.07 7
.0 

### '9.3 1.3 1
.02 11 3 6 .3 19.4 1.1 111 Invakt dn la .8.B 1.7 0 .71 117 3 .' IB.O 24 ' 22 106 28 .00 

# ... -0 .07 66 

### '9.3 1.3 1
.02 112 5 .9 1 9
. 3 1 .1 111 I nvalid da l3 

### ' 8.6 •.7 070 117 3 .8 1 8.0 Z 4 122 107 28 .03 

### 46 .0. 0 7 6.4 

### '9.3 . _3 1.02 I II 5 .' 19 .3 1
. 2 110 InvaIid da la 

### 18.6 1.7 0 .71 116 3 

## . e 1 8
. 0 

### 2A t 21

Pago 1**.:** TOAS 

# I NOx CEMS CAHA
.. "(J 4789 :;,ooo .5(d
. 08 

### STACK A- 

### inputs Tab !

el S 

### STACK B- 

### inputs Reo;;ocdcd Data**'5-rr ute<Nc:a:;Ws** 



### STACK C·l nputs RECORD ;uPrc: :.sj"HTmp_F

### ~13t.l**(:P Av** **~vg(l** 

# ""-""" "pJ "-,,,,,,,...,.,,,,,, _ ,,,,'"'P.' .''''''''.''''9\'**"".".'<'""".""""'~'""-"~'** RN Wig Deg F nH2.0 

### PPfT\Dfy



### 28.23 28
.22 28.21 

### 2820 28.19 28.16 28
. 17 28.17 28
. 16 20 28
. 15 20 28.14 20 28
. 1 3 20 28
. 12 20 28
. 11 20 28 .1 1 

### 20 49 28. 1 0 21 50 28. 10 21 51 28.ca 21 

### 52 28
.ca 21 

### 53 28
.07 

### 22 54 28
.05 21 55 28.05 20 56 23.04 20 57 28.03 20 

## sa 28.03 

### 20 59 28,03 19 60 28.02 1 9 28.02 19 28.02 19 28.02 1 9 28.01 1 9 28.01 16 28.0 1 16 28.00 19 28.00 20 

### 28
. 00 20 28
.00 21 

### 28.00 22 28. 0 1 

### 22 28
.00 

### 23 26
. 1):,1 23 26
.00 23 28
.00 2:J 

### 26
.0'2 N 28 .01 

### 28 28.0'2 23 26.02 2 5 2.3
.02 26 28
. 02 26 

### 2.8.02 

### 2Ei 28.02 3 1 28.02 35 za.02 S4 

### 2.8.02 32 28,02 

### 33 28,02 S4 2.8.03 35 28.03 

### 30 28
.03 36 28.03 41 28.03 42 28
. 02 -!3 28.03 45 97 23.03 '6 99 28
.03 47 99 

### 28
.03 47 28
.03 '6 28.03 45 

### 28
.0'2857 46 25
.03 "'" 

### 28 .02 45 28 .03 47 28
.03 "'" 

### 28
.03 46 · 0.14

· 0. 1 4 ·0. 1 5 -0.14 -0
. 1 5 -0
. 15 ·0.14

· 0 .14 -0
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. 14

· 0
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. 1 4 -0.' 4 -0.1 4

-CU4 -0
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. 14 -0
. 14 -0. 14 -0. 14 -0.1 4

-0
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. 14 -0.14 -0.14

· 0.14 -0. 14 -0. 14 -0. 14

· 0. 14 .(1
. 13 .(1. 1 3 .(1. 1 3 .(1
. 13 .(1
. 1 3 -0. 1 2

· 0
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. 12

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· 0 , 10 -::1. 10

· 0.09 -0
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### -0,09 ·0
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### -0.03 -0 ,03 -O.C9 -O.OS

· O

.OB -O.CS -0
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### ·0.08 -0
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· 0.0 7

· 0. 07

-0
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19.2 19.2 19.2 19.2 19.2 19.2 19
.2 19.2 192 1 9.2 19.2 19
.2 1 9
. 1 19
. 1 19
. 2 19
. 1 19 .1 19.1 19.1 19 .1 19.1 19.1 19.1 19.1 19.2 19.1 19.2 19.1 19,1 19.1 19.1 19.1 19.1 19. 1 19.1 1 1U 6 . 9 11
.2 16 .0 19 .4 19.5 19.5 19
.4 19.4 1 9
. 5 1 9
. 5 19
. 6 19.6 19.6 19.6 19.6 19.3 19.0 19.0 19.3 19.6 19.1 18.9 18.9 18.8 18.8 18.7 18.7 18.5 19.3 19.3 19.3 

### 19
. 3 19.3 19
. 3 19
. 3 19
. 3 

## IJ!-3 0.91 0.902 0.89 0.89 0.89 0.91 0.91 0.91 0.90 0.92 0.90 0
.90 0. 9 1 0
. 9 1 0. 92 0
. 91 0
.9 1 0
. 90 0
.92 0
.90 0.91 0
.90 0
.90 0.92 0.91 0.91 

## o ,£-oJ 0.91 0.00 0.89 0.90 0." 0.91 0.88 0.90 0.90 0
. 90 0
. 89 

### 0
. 86 0
. 89 0
.90 

### 0.00 0. 87 0
. 89 0. 91 0.S2 0.93 0.92 0.91 0.91 0,91 0.9 1 0.89 0.92 0.91 0.94**o.~** '.00 0.95 0.96 

# '.00 1.05 '.02 '.02 '.02 

## '. 03 1. 02 1.02 1. 0 1 1.02 

### '
. 02 '. 02 1. 02 5 , 4 

## 5
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### 56 57 

### 5
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### 5
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### 19
. 3 19
. 3 19
. 3 19
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. 3 19,3 

### 19.3 

### '9.3 19
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### 19.3 19.3 19.3 19
. 3 

### 19.3 19.3 19.3 19
. 3 19
. 3 '9
. 3 19
. 3 19
. 3 19
. 3 19
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### '9.3 19, 3 19
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### 19
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### 19.3 19.3 19.3 19.3 19
. 3 19.3 

### 19.3 19
. 3 19.3 19
. 3 19 , 3 19
. 3 19.3 

### 19.3 19.3 19.3 19.3 1 9
. 3 19
. 3 19.3 19
. 3 1 9
. 3 19
. 4 19
. 3 1 9
.3 0.95 0.97 0.96 0.95 0.95 0,95 0,97 0. 96 0.96 0.96 0.96 0
. '" 0 .95 0
. '" 0. !i6 0
.97 0. 94 0
.94 0 .93 0.94 0.96 0.96 0.96 0.S3 0.93 

## 0." 0.87 0.82 0,82 0.90 0.96 '.03 1.03 1.02 1.03 0.99 0." 

## 0
."
'
.00 1
. 24 1 .0 1 0.79 0. 67 0
. 69 0. 9 1 0
.S3 '.03 1. 0 2 1.03 1.C9 1.11 109 In
...

### aid data 103 I nvaid dilla lea InvaPd dala 109 tnvatd data 103 lnval'ddara. 103 lnva6. d data lC3 lnvaIiddata lC9 

### invalid data 109 1nvaI:dcb1.3. 18.6 109 fn\taid 

### data 18
. 6 109 JrJv4i'1d data 18.6 109 

### IImid d.iltl 18.8 109 InvaM:I chta 18.6 109 Inva!id d.lIa 18,6 109 l nwid d.3ta 18
. 6 109 I nvaid data IS.6 109 Invald data 1S
. 6 109 l nvald data 18.6 109 ! nvaid d31a 

### fS.6 1 1 0 

### l nvald d31a 

### ,a6 1 1 0 I nvaid data 18.6 109 Invald data 

### taB 109 Invaid data 18.6 109 lrwaid diJIIll 18.6 109 Imaid data 18.6 109**I~datll** 18
. 6 109 Inv3id daot3 18
. 6 109**aid** data 18
. 6 109 Invakl data. 18.6 103 I nvaid data 18.8 lC3 Invaid data lS
. 6 1 C3 In vard data 18.6 lC9 Invaid dat;a 18.6 lC9 irlv'»d data 18.6 103 Invat:ddata 18.6 109 InvaIld data: 18.6 109 IrMIIid dilla: 18.6 110 Invalid data 1B
. 6 110 

### Invalid data 18
.6 110 Invalid dilla 18.6 110 In,, <tid data 18.6 109 Inv3id data 18
. 6 110 

### Inv a.'id datil 

### laB 11 0 IIMUd data IS.6 1 10 

### jnva5d d3Ja 18
. 6 11 0 J nva!id data 18.6 1 1 0 1 nva5d daIa 18.6 \ 1 0 Invald data 18.6 109 Invalid lbla 18
. 6 

## no I nvaid dllla 1B. 6 113 I rwaid data 18 ,6 115 Invaid data 

### la6 "3 l nvaid data 18.6 112 Invaid data 18.6 110 IrMdid dalll 1S.6 " I 

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,,, Invaid data lS.8 111 Invalid cata 18
. 6 110 InoJajd tiilta 18.6 "0 Wwal' da'ata 18.8 111 In vnt d tiaUl IS.6 III 

### 1nvaIld d.1!a 18.6 1 I 1 In vatid data 18.6 111 InvafId data IB.6 

### '" InvaIid data 18
. 8 ' " invalid data 

### las 11 0 lnvaIid da1a 18.6**IC~** Invalid data 1S
. 6 110 lnvaIid d.lla r8.6 1 10 

### InvaIid data " ,6 I I I lnvaIid d:lla 18.6 111 I nvalid dala 18.6 11 0 

### Invatid da.ta 18
. 6

Pago I 

### 0.84 0
. 86 O
. BS 

### 0
.84 0
.84 0
.84 0
.00 0
.85 0
. 85 

### O
.SS 0
.85 0
.85 0
.86 0.84 0 .85 0." 0
. " 0
. 84 

### 0
.85 0. 85 

### 0." 0.65 0.67 

### 0
.86 0
. 65 0
. 85 

### 0
.86 0
. 85 0
.86 0
.86 0.85 0.86 

### 0
. 85 0
.85 

### 0
. 85 0
.82 0
. 61 0
. 79 0
.77 0 ,65 

### 0
.70 0
.80 0.82 0.80 0. 79 0. 82 

### 0
. 82 0. 82 0
. 61 0 .79 0 .81 

### 0 .7 9 0
.80 

## o .n 0
.80 

## o .n 0
.78 0
.79 

## o .n 0
.76 0.75 

### 0.76 

### 0.75 0
.74 

### 0
.72 0
. 73 0
.72 0.72 0.71 0.71 0.71 0.7 1 

### 0
.70 0
. 71 

### STACK 

### 0- inputs 02_Avg(4):x>2_Avg(4.irf'Iow4fid1:Tmp_F _""'0 (4) P<enIOoy
_ 

### nH20 0.., F

# ~**~g A~ '9** **~::~ iajl~ii~~~** **::::~**

18.0 2." 78.0 2.4 18.0 U 18.0 2.4 18.0 2.4 18.0 2.4 140 2.4 18.0 2.4 

### 18.0 2.4 18.0 2.4 18.0 24 18.0 2.4 18.0 2.4 18,0 2.4 18.0 2.4 18.0 2.4 f8,D 2.4 18.0 2.4 18.0 2
. 4 18.0 2
.4 faD 2
.4 IB.D 2
. 4 18..0 2
.4 18.0 24 lao 2.4 18.0 2
. 4 18.0 2.4 18.0 2.4 18.0 2.4 18.0 2.4 1B.0 2.4 18.0 2.4 18.0 2.4 18.0 2.4 18.0 2.4 18.0 2.4 18.0 2.4 18.0 2.4 18.0 2.4 18.0 2." 18.0 2.4 18.0 2.4 18.0 2.4 18.0 2.4 18
. 0 2
.4 18..0 

# 2." 18.0 2.4 f8.D 2
. 4 18.0 2
. 4 18.0 2
.4 18
. 0 2
.4 18

. 0 2 ." 18.0 2.4 18.0 2.4 18.0 2
.4 18.0 2
. 4 16.0 2.4 IB.O 2.4 IB.O 2.4 IB. O 2.4 18,0 2.4 1B.O 2.4 18.0 2.4 18.0 2.4 18.0 2.4 

### 18.0 2.4 18,0 2.4 18.0 2.4 18.0 2.4 18.0 2.4 18.0 

### 2.4 tao 2.4 

### 18
.0 2
. " 18.0 2
.4 

### 18.0 2 ." 18
. 0 Z
... 

### rao 2." 18
.0 2
. " "
. 50 .0
. 50 

### ·0.50 .0
. 50 >2' 123 123 

### 123 123 

### 123 '23 123 

### '23 '22 123 123 

### 123 123 

### '23 '23 123 123 123 123 

### 123 123 

### '22 123 

### '22 122 122 

### '22 '22 

### 123 122 123 

### 123 123 123 

### '23 '23 124 Stac k A • System 

### Bias Check

, 24 Stack A
. 

### System Bias Check '24 3 - Sy stem 

### Bias 

### Check I Stack 0 Ai r 

### Flow Sensor' 123 Stack 

### 0 1M 

### Row Sensor otf-ine 1 22 :: • Sytl." 

### Sial Check I Stac k 0**~** Flow Sensof ' 1 22 ) - 

### System 

### Bias 

### Check I Srack 0 All 

### Flow Sensor' 

### 123 Stack 

### 0 M Raw**~** 0If .ft 

### 123 

### S&Iick 0 

### Nt 

### Row 

### Sensor**Off~ .**  

### '22 122 122 12 ' 12' >2' 

# ,,. 123 

### '23 '20 

# "'" '20 

# '2' '22 '21 

### '20 >2' '22 122 

### '23 '23 

## t»lCO/! 122 

### '22 

# '2' '22 

# '2' '22 '22 

### >2 1A ecOfdcd DaLil 15- mnule .lVerag es. 

# I STACK A- 

### inputs STACK B- 

### inputs STACK C· 

### inputs STACK 

### D- inputs TOA5 N Ox C E P.1 S C R1 CQ'J 4789 =llC·J().S!d.08 Tabl e 1 5**TI~ .~** **STAI.4P** RE C CRD a rPrO'is_A\ rTIT'.p_F_A'51aticP**.,, vg**  02_Avg(1) X>2

_Avg(1 J rAow 1

_A\'{Tmp

_ Fj.;"30:2_Avg(l**CX!:_Avg(2)~2_Avg(2.ifF!o'.v2_Av.Tmp_F** _Av 

# so**~1** 

### 02 ii;(3)X)Q [k "T

"<1 ' 0 2..Avg(1**02..Avg(4)~02_Avg(4.ifAowUd;Tmp_F** _Avg (4) 

### 1 5 AN**Hg** Deq F**I~H20** ppmD<y PrcntDry PcntOry 

### "H2O Dog F ppmOry PrcntOry PcntOry in H20 

### DogF 

## ....."'Y. oPiadOry PcntOry 

# "H20 ' Dog F 

### .. mO<y PrcntDry PcntDry 

### DogF A', Avg A'" A'9 A'9 A'9 A vg A vg Avg A", Avg A', Avg ' A A A ' A A Avg Avg Avg Avg Corr n lttlts 

### 10. 28.OJ 

# '" -0.07 6.8 19.3 1.3 1. 01 11 2 6.0 '8.6 1.5 

# '" Inv aid data 18.6 

# I .> 0
. " 11 7 3.6 18.0 2.4 123 

## i2!Cotoata: lCO 28. ().l 

# '" -0.07 6.6 19.3 1.3 0.9S 113 5 .8 '8 .6 1.5 III Invaid d ata 18 .5 ' .7 

### 0.67 118 3 .2 18.0 2 .4 1 23 11 0 28. ().l 

# '" -0.07 6.2 19.3 1,3 0 ,,", 11 3 5.4 18.6 1.5 '11 Invaid data 18 .6 1 ,7 0 .66 118 2 .9 18.0 2.4 124 111 28.04 

# '" -'J.o7 6.0 19.3 1.3 0.99 113 5
. 1 '8.6 1.5 111 Invaid data 18 .6 1,7 0 .6 9 118 2 .7 18.0 2.4 124 11 2 28. 04 43 - 0.08 6 ,0 19.3 1.3 1 .02 113 5 , 1 18.6 1.5 111 Vlvaj j data 1 8.7 1 ,6 0 .73 118 2 7 18.0 2.4 124 113 23 .07 42
-0.05 6 .9 19.3 1.3 0 .92 11 1 5
. 8 18.6 1.5 109 Iovat j da: a la4 

### 2,0 0 ,66 115 2 .6 '8.0 2,4 122 

### O2IC02DOia ,f", 0 28 .05 41 -0 .08 4 ,2 19.3 1.3 1 .02 112 3 .9 l aB 1.5 111 lnvaJ j da ! 3 'S.4 

### 2,0 0 .75 11 8 3 .1 7 .5 2
. 7 124 Stadt 0 • Sy s !am Bia s Crift Ctl4c k 1 2a.OS 36 -0.08 7 .0 19.3 1.3 0. 99 115 6 .0 18.6 1.5 113 It'lvaMj d aL3 1S .4 

### 2 .0 0 .74 11 9 2.6 18 .2 2.6 125 SbcK C • SYS f lllO'lBias Onl l Cl'ieck 2 2.0 .06 36 -0.08 6 ,1 '9.3 1.3 1,02 113 SA '8.6 1.5 112 Invalid data 

## ts» ZO 0 .75 118 25 18 .0 2.5 124 Stack C • Anatyzer Cal bration 3 :?a .06 35 -0.08 6 .9 19.3 1.3 0.>9 114 B.2 18.6 1.5 112 Invaliid da l a 18.4 

### ZO 0 .74 11 9 26 18 .0 25 1 25 S l 3Ck C • SY Sl -rTl Bias Chec k 4 28 .06 

### 34 -0.09 6,3 19.3 1.3 0 ." 113 4 2 18.6 1.5 112 1nvaIid <hla. 18.4 

### 2.0 0 .72 119 2 4 18,0 25 126 S I:JCkB • Sy S!(,,", BQs C n n CtI tlCk. 5 29.0 7 32 -0 .09 

### 5
.0 19.3 1.3 1,00 113 3 .9 78 .6 1.5 1 12 lnvaid <hI a 18.4 

### 2 .0 0
. 74 1 19 21 1 8.0 2.5 

### ' 26 Slxk A· System Bi:l s Onlt Chec= il. 6 28. 07 

# so -0
.09 4 .2 19.3 1.3 0 .99 113 4 0 78 .6 1.5 11 1**1~ da1a**  18.4 

### 2 .0 0
. 74 119 20 18.0 2.5 126 7 26
. 07 30 -0 ,09 4 .7 19.3 1.3 1.00 

### ' 14 .. . 2 1S .6 1.5 1 12 lnv .Dd data 18.4 

### 20 0
. 75 1\9 1 .9 i 8.0 25 

## o.s 1 28 8 26
. 07 31 -0 .10 ':'8 19.3 1.3**9~** 115 . 2 18.B 1.5 1\3 I nvaSd data 18.4 

### 2 ,0 0
. 74 121 1.7 16.0 2. 4 0. 95 128 9 

# ae.ce 3
. -0
. 10 3A 19.3 1.3 0 .9 7 11 3 3 .1 18.B 1.5 1\ 2 1 nv.Ud dat a 18.4 

### 2
.0 0. 74 1\9 1.7 1 8.0 

### 24 0. 96 127 

### 10 28 .0 7929 29 -0
. 10 33 19.3 1.3 1. 00 11 2 32 18.6 1.5 ' 11 :nva:id data 18.4 

### 2 .0 0. 78 1\8 1
. 8 18.0 2.4 0 .97 1 26 11 28 CO 29 -0
. 10 3.6 19 .3 1.3 1
. 02 1\ 2 3 .4 18.6 1.5 1 1\ Inv3id dola 18.4 

### 2
.0 

# o .n 118 1
. 9 1 8
.0 2. 4**0.9~** 1 26 12 28.C9 29 -0 .10 '3 19.3 1.3 

### . 0< 1\' 4
.0 18.. 1.5 1\ 1 tmla\d data 18.4 

### 2 .0 0 .60 11 8 2 ' 16 .0 2.5 1 .01 1 24**2a .1~53** 

. 3 28 .09 29 -0
. 1 0 6.8 19.3 1.3 1. 00 1\4 

## e.i ts« 1.5 1 11 rmaid data 18 .4 

### 2.0 0 .7 9 11 8 2 .6 16 .0 24 0.9 :1 ' 24 

### 14 28
.09 27 -0. 10 6 .4 19.3 1.3 

# Le v 114 5 .6 1 6 .6 1.5 112 ""'alid dala '8.4 

### 2 .0 

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. 01 125 31121080:00 

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. 3 18.6 1,5 0.78 

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21080 : 30 2 4 28.09 28 -0.11 53 19.3 1,3 1
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### 31 ' Z·08 " : ..;s ,3.1 1 20'00 12 :00 31 1 20'00 1 2: 1 5 

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### STACK C- 

### inputs

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### STACK 

### D- inputs**02....Ay.g(4j~02_Av 9l** **.¢..ifAawUd;TITIfl]**

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2a, 1 4882353

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### inputs STACK B· 

### inputs STACK C- 

### inputs STACK 0- 

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;08 12:45 73**.S** 

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### svsren &as D nU Chec k 3/ 12J08 13 :00 74 27
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### 12' 3/ 12':08 16:30 88 27 .90 

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# ., 27
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. 1 3 1 0
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# _ data
18 .5 0
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.00 122 3 ' 1 3r'OO 0: 30 1>0 27
. 77 2 ; -0.12 7... 19.3 1.3 0. 92 111 6 .0 18.6 1.5 0. 8 7 110 In vallddal a HJ.4 0.8 1 16 3 .1 18.0 Z4 0 .99 122 31131

000 :45 121 2 7
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. 76 2 5 -0.12 63 19.3 1.3 0 .91 111 5 .0 18 .6 I.S 0.76 110 lnvakl do1! a 1 8.4 0. 81 

# " ' 2 7 18 .0 2.4 0 .98 123 3o'1 3i081:15 123 27 .75 2 ; -0.12 6.1 19.3 1.3 0.93 110 '.8 18.6 I.S 0.75 110 In vatJdda l;Ji 1 8.4 0.81 11 6 28 '8.0 2.4 1 .00 1 22 3' 13<

'08 ' :30 124 27 .75 

## zs -0.12 7.1 19.3 1.3 0.93 111 5.6 IS.6 I.S 0.75 110 lnvaIid d al a 18.4 0.62 11 6 2. IS.O 2.4 1. 01 1,23 3'1 31C8 1:45 125 27 .75 25 -0.12 8.9 19.3 1.3 0.91 III 54 18.6 I.S 0,74 110 Invakl dal a 18.4 0.8'J 11 6 2
. 8 18.0 2.4 0. 99 1 23 1' 1 3/

08 2:C-o 126 27 ,7 ':'- 26 -0.12 63 19.3 1.3 0.94 110 4 .' IS .6 1.5 0.75 110 Lnva!id daIa 1 8.£ 0.82 116 2 .6 18.0 2.4 UX) 1 23 3." 3<'

082 :15 127 27 .73 

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.7 f8.0 2.4 1.01 123 3/ 1 31C82 :30 128 27
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C 8 3 :30 . 32 27 .72 2 5 -0 .12 75 19.3 1.3 0 .9 3 113 6 . 1 18.6 

### I
. • 0.7 4 III I nv<Uddat3 18 .4 0. 82 11 6 3 .5 18 .0 2.4 1.0 ' . 22 3.'1 3ICS 3 :45 . 33 27
. 72 26 -0
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.92 113 6 .':' 18.6 I.S 0 .7 4 

### tt t l nvaid 

### dal.1 18 ,4 0 .8 1 117 3 5 1S0 2.' 1.00 122 3' 1 J.'08 4:00 1 34 Zl .7 1 

### Z7 -0
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. 74 III I nvaic1 data 1 8 .4 0. 91 117 2
. 18.0 2.4 1 00 12 ' 3 '131C 8 4 : 15 1 35 2 7
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. 11 6 .4 19,3 1.3 

## a." 117 

## -cs 18 .6 I .S 0
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### l m'aid data 1 8.4**.7** 1 22 

### 21 18 .0 2.4 1 .01 129 3113 08 5 :00 1 38 27 .69 33
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# ........

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### 1 21 22 18.0 2.4 1
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·005:30 140 2 7
. 69 33 -0.10 6.7 19.3 1.3 0 .95 115 5 .8 18 .6 1.S 

# on 114 Irwaild data 18
. .. 0. 82 120 30 16.0 2.4 1
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. 1 '8.0 2.4 1.0 1 126 3/13:086:00 142 2 7
. 69 33 -0.10 7.3 19.3 1.3 094 116 6.8 18,6 I.S 0.74 115**::I at**  18
.5 0.81 120 4
. 6 18.0 2.4 1 .00 125 3"1J,'oe6:'5 143 27 .6 9 33 -0.10 7.1 19.3 1.3 0 .94 116 6.6 16.6 I.S 0.75 115 

# "''''' 

# .... 18 .5 0.83 120 ' .7 IS.0 2.4 1.00 125 3.'130086:30 

# .44 2 7
. 69 33 -0.10 6.9 19.3 1.3 0.93 117 6.3 18.6 I.S 0.73 115 InvaIId dala 18.4 0.83 .20 '
.2 18.0 2.4 1.00 1 25 3' 13"'08 6:45 145 2 7.09 34 --0.10 6.8 19.3 1.3 0.93 '16 82 18.6 I.S 0.73 115 InV8llCl data 1 8.4 0.81 120 3 .4 18.0 2.4 1.00 126 3I 13<

'C6 HiJ 140 2 7 ,69 34 -0.10 0.9 19.3 1.3 0 92 116 62 18.. 1.S 0.73 115 

# """" da
.. 1 8.4 0.81 121 3 .0 18.0 2.4 0.99 127 3.' 1 3108 7 :15 147 27 69 34 -0. 10 8.4 19.3 1.3 0
. 91 116 5 .7 18.6 I.S 0.73 115 InvaIid d a :a 18 .5 0.80 121 2 5 18.0 2.4 0 .99 128 31130-'087:3:) 

# .48 27 ,6 9 34 -0. 10 5 .5 '9.3 1.3 0. 92 116 4 .3 18.' I.S 0.78 11 5 

### lnV3id

### Ga te. 18 .4 0. 79 122 2. 0 18.0 2.4 0.99 '29 3113,'C87 : 45 

# 14
. 27 ,6 9 33 -0. 10 

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### '8 .6 I.S 0. 80 115 

### 1nv aJ'd

### o:a.: a 18.4 0130 12 1 1.6 18.0 2 .4 0 .99 12 8 

# I STACK A· 

### inputs STACK 8- 

### inputs NCx CEMS CA,oao 4789 =:jlC00.S1d.08 Ta,b(015 Rcco:dc.dDaI.:l lS-minule av«age:s



### STACK C- 

### inputs TQAS**TIMESTA.'.~P** T5 RN i"lHg 

### Deg F ilH20 ppmDfy PrcntDry PcntOty inH20 O eg F ppmDry PrcnlOry Pcn!Ory inH20 Deg

# ~ 

# - 

# -**~ ~** **~ ~ ~** **~ ~ ~**  

# - RECORD ntPr«iS_ AHTmp_F_AI31<l1:P_AV ;? 02..Avg ( 1 02J\vg(I):i02_Avg(l .i. rAow1

_ A
.....T/T'4l

_F

## ~... i02_Avg(1

## OZ-Ayg(2PO~:U\vg(2~rA0w2_A\(TIT'4>~~F**~~ ~**  

# • •**IIII!I!!I!!!!!I!I~..** 72 28
.00 30 -0.11 3.3 19
. 3 1.3 1 .03 111 4
.2 18.6 1.5 0.78 3/12/0812:45 73**:;: .S** **~** 29 -0.10 3.6 19.3 1.3 1.03 111 2.8 18.6 '
.5 0.84 3/12J0813:oo 74 27 .5 9 

### :2'9 -0. 10 3.8 19
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. 03 111 3.0 18.6 1.5 0.91 31fZ:C81J:IS 75 27.98 29 -0.1' 4.6 19
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. 3 1.00 112 3.6 IS.6 1,5 

## a.eo 3112iC81J:30 76 27.97 30 -0.10 3.8**19.~** 1
. 4 1.02 112 3 ,0 18.6 1 ,5 0.89 3112,0813"45 T7 27.96 31 ..IJ. l 0 3
. 8 19.':' 1.3 1.03 112 2.9 "
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.5 0.79 3Il2tOS 1 4:00 78 27.96 30 -0. 1 0 4
. 6 19.4 1.3 1. 0 1 11 2 3.5 18.8 ' .5 0.79

31121O!! 15:00 3112'-0815:15 3,112'-08 15:30 3/12i0815:.45 3/12,'0816:00 3/12,'0816:15 3/12':08 16:30 :1'12':03 16:45 :1'1Z.'CO 17:00 :1 ' I2fDa 17:15

3 ' 1 31'Oe0: 00 3!131()80:15 3 ' 1:31000:30 3/1 3/08 0:45 3/1 31 08-1:00 3'131081:15 3113108 1:30 3113tC8 1:45 3113/08 2.C-o 3.'1 3106 2:15 31 13108 2:30 3113108 2:45 311 3108 3:00 31131C8 3:15 31 131C83 ::iO 3 ! 131C8 3 :45 311 3108 4 :00 3 ' 131'C 84 : 15 3 ' 131094:30 3113'094:45 3113 ·08 5:00 3113'08 5:15 311:Y095:30 31131085:45 3/13,'086:00 3-'13.' 086:15 3'13. '08 6:30 3,1131086:45 3113108 7:riJ 3-'1 3108 7:15 311 3108 7:3J 31 13'C8 7 :45 79 BO B' B2 B3 85 86 B7 B8 

# " 

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### , ,5 0.75 27
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### t.5 0.81 27
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. 84 22 -0.13 4.1 19
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. 84 22 ·{).14 4.2 19.3 1.3 1.01 110 1.3 18.5 1.5 0.65 27
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. 75 :25 -0.12 7.1 19.3 1.3 0.93 111 5.6 18.6 1.5 0.75 27.75 25 -0.12 6.9 19.3 1.3 0.91 111 5.4 1S.6 1.5 0,74 27 ,74 26 -0.12 6.3 19.3 1.3 0.94 110 4,9 18
. 6 1.5 0.75 27
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### 148 1.5 0. 74 27.70 32 -0.11 6,4 19.3 '
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### J.3 -0.1 i 6,4 19.3 1.3 0.94 116 5.1 18.8 1.5 0.7 6 27
.69 

### J.3 -0.11 6.3 19.3 1.3 0.::4 tiS 5.1 

### t8.8 1.5 0.7 4 27.69 

### J.3 -0.10 0.6 19.3 1.3 0.94 115 5.6 18.8 1.5 0.74 27
.69 

### J.3 -0.10 6.7 19
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.69 34 -C.l0 7A 19.3 1, 3 0.94 116 6.7 1S.6 '-5 0_75 27 .69 33 -0.10 7.3 19.3 1.3 0
. 94 116 6.8 18
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### J.3 -0.10 6.9 19.3 '
. 3 0.93 117 6.3 ".6 1.5 0.73 27.09 34 --0.10 6.8 19.3 t.3 0.93 116 6 .2 18.6 1.5 0_73 27
.69 34 -0.10 0.9 19.3 1
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.69 34 -0.10 

### 6A 19.3 1.3 0
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.69 34 -0.10 5.5 19.3 1
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### Invalid data Invaliddala lnvalid d.1la II'IVUi d.1la l nvaid d.lta Invaid data 1nvaId dala 1nvaId dola



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## '.9 '.9 1.9 1.9 1.9 0.80 0.78 0.78 0.77 0.79 0.78 0. 77 0.78 0.79 0.78 0.77 0.77 0.76 0.77 0.77 0.77 0.78 0.79 0.79 0.77 0.77 0.75 0.72 0.77 0."" 0.79 0.90 0.78 0.79 0
.80 0.81 081 082 0.83 0.83 0.82 0.82 0.81 0.31 0.80 0.65 0.82 0.82 0.8' 0
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# I.. STACK 

## D- inputs 02_Avg(4)::Oi..A...g(4.arF1ow4_A>dI:Tmp_F**~vg(4)** 

### Prc-nlOry PcnlOry I\H2O 

### Deg F Avg Avg Avg 17
.9 2.4 1.01 125 17 .g 2.4 1.01 125 10
. 8 

### 1.7 1.00 124 IB.O 2..4 0.99 124 18
. 0 2.4 1.01 125 18.0 2.4 1.00 124 18.0 2.4 0.99 124 ,8.0 2.4 0.99 124 18,0 2.4 0
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.93 l za 140 2.4 0.93 1:'<6 

### 18.0 2.4 0.95 1 25 18.0 2.4 0.99 125 18.0 2.4 0.98 124 1B.0 2.4 O.SIS 124 18.0 2.4 0.98 123 

### '8.0 2.4 1.01 122 18.0 2.4 1.00 121 18.0 2..4 1.00 121 IS
. 0 2..4 0.9a 121 18.0 2.4 0.98 122 

### 18.0 2.4 0.96 123 18.0 2.4 0,94 124 1S.0 2.4 0.98 124 18.0 2.4 1.01 123 18.0 2.4 0
.99 123 

### 18.0 2.4 0
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### 18.0 2.4 1.01 123 18 .0 2..4 1
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### 18.0 2.4 1.01 121 18.0 2.4 1.02 122 

# ".0 2.4 1.01 121 1S.0 2.4 1.01 121 18.0 2.4 1.01 122 1S.0 2.4 1.01 122 

### 18.0 2.4 0.99 122 18.0 2.4 1 .00 122 '8.0 2.4 1.00 120 18.0 2.4 1.00 121 18.0 2.4 1.01 121 18.0 2.4 1.00 1:21 

### 18.0 2.4 1.00 122 18.0 2.4 1 .00 121 18,0 2 .4 1 .00 1 22 18.0 2.4 0.99 122 18.0 2.4 0_97 123 18.0 2.4 0.98 123 18.0 2.4 1.00 122 18.0 2.4 1.01 123 1S.0 2.4 0.99 123 

### 18.0 2.4 1.0'J 123 

### 18.0 2.4 1.01 123 1S.0 2.4 1.02 122 18.0 2.4 1.01 122 

### 18.0 2.4 1.01 122 18.0 2.4 1.01 122 18.0 2.4 1.01 122 18
. 0 2.4 1.00 122 18.0 18
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### 18.0 18.0 18.0 IB.O 18.0 18.0 18.0 .&0 2.4 

### 2.' 2.' 2.4 

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## 2.' 2.4 2.4 2.4 

## 2.' 2.' 2.' 2.' 1.00 1.01 '- 01 1 .01 1 .01 '.00 1.01 1.01 '.00 1.00 1.00 1.00 0.99 0_9:1 O.g:1 0.99 

# "
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### ' 29 '28 '27 

# ,,. '2. 125 125 125 126 

### '27 

### 128 '29 

# '2' C ommns Stack C - SysTem Bias O rJ t Check Smc"- 0 • System Bias Drill D-:eck

System 

### Bias O ril CheckRecorded D era**s-. e3\.** **'e' 3;cs**  

# I STACK A- 

### inputs STACK B- 

### inputs STACK 

### C- inputs STACK 0- 

### inputs TOAs N Ox C EMS C A1OCO 47 89 :n OOO. S td.06 TOO:61 5 T1.'

:ESTAt.lP RECORD arP rn s_ A\ rTmp_F _ABta1icP**_A \'** **02 ..A** **vg: ( 1**  02

_Avg:(1»02_Ayg(1 .irAow'l _A-..; TmpJ-A Y 302.. A \'g ( 1 02_Ayg(2):02_A...g(2.irAov."2_Av:Tmp_F_Av 

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### 1 .S 0 .77 112 I n vil 'c1 dala 18. 4 Z' 0 .8J 

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### 1 .S 0 .76 112 f rwaid data. 18.4 2' 0 .79 118 0.0 18.0 2.4 0.99 123 3.'l:J

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### I.S 0.88 110 In vafddat a 18.4 

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. 77 11 6 2 .3 17.8 

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### 33 ' 9.0 1.6 0.9 5 11 0 

### Inval:d data. 18A 

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### 33 \9 .0 l.7 0.87 

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. 11 4.3 19 .2 1.4 0. 92 11 ' 36 1 9
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# I., 0 .79 109 InvaIicl da ta 18.4 

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### 2. 0 0 .78 

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### 200 2 7 .8 1 28 -0 .1 1 ':',9 19 .2 1.4 0 ' 2 

# " ' '2 19 .0 1.0 092 11 0 Invalid dat a 18 .4 

### 2 .0 0 .80 

### ' 16 2':' 1 7.8 2 .8 0.99 '24**3J 1.1'C8~** **()-45** 20 1 2 7
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# " ' 38 19 .0 I
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. 11 3 .8 792 

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### 2"..4 27
. 81 28 -0 .1 1 35 192 1.4 0 93 ' 11 

### 32 1 9
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### 20 0. 60 Tl6 2
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# ' " lnv.1'idd all:l 18.4 

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. 8 1 116 Z I 1 7 .8 2.6 1.00 ' 25 3J1.1 C922 :OO 

## zoe 27 .80 28 -0 .11 31 '9.2 I
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### 2
. 0 0. 82 116 2 .0 ' 7.8 26 

### '. 02 1 25 3J 1 3.C9 22 : 15 207 2 7 .S :> 28 -0 .1\ 4' 19 _2 1.4 0 .97 109 3 7 1 9.0 I 

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### 20a 278 1 28 

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### 20 0. 82 

# " ' Z. 17.8 

### 2.8 1 .0 1 1 23 3. ' l.1 C822 ;45 20' 27 .8 1 27 -0.1 1 65 192 1.4 1. 00 

# ' " 5 .7 1 9.1 ' .6 1
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### 20 0 ,S 1 11. 2 .8 1 7.8 26 1.0 1 12 .:. 3Jl3.CS23 :o:J 210 27 .80 27 -0 .12 6 0 19.2 1.4 092 

# "' 5 .' 19 .0 1.6 1.00 "0 J nviUd d3! a 18.4 

### 2.0 O S2 

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### 20 0 .S 1 11 6 24 17.8 2. 6 1
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### 2
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### lnvaJd data. 18.4 

### 2. 0 0
. 84 11 6 25 11.8 2 .' t.Ol 1 23 3.' 14.'030 :00 214 27 .60 26 -C. 12 7 .0 19.2 1.4**.~** 11 0 6 .3 19. 1 15 1. 03 "0 lrwaid d<l ta. 18.4 

### 20 0
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# '" I nv;Del da l.a 18.4 

### 2.0 0 .6 1 

# "' 3.2 17.8 2 .6 '.00 1 24 2 18 27 .81 25 ·0 .12 6.5 192 ,.4 0.9 1 11 2**.~** 1 9.0 1. 5 0 .87 

# "' I nvaid da ta 18.4 

### 2 .0 0
.50 117 27 11 .8 2.6 0.98 1;;:5 3. '1 4 '

08 0 : 45 217 27.S1 26 -0.13 5.0 192 1.4 0.94 

# " ' 4.4 19.0 1.6 0.89 '11 I nvalcldata 18.4 

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### 2 .0 0 .83 116 2. ' 17.8 2.6 1.01 12.5 3. ' 14':08 1:15 219 27.60 25 -0.13 4.' 19.2 1.4 0.97 '09 3. 7 1 9.0 1.6 0.75 "0 lnvakl da ta 18 .4 2 .0 0
. 84 

### '16 Z2 17.8 2.6 ' .03 '24 3J14iC 91 :30 

### 220 27.SJ 26 -0.12 4.4 19.2 1.4**O.~** 11 0 4 , 1 9.0 1.6 0.S9 110 l nva'td data 18.4 

### 2.0 0 .S3 116 2 3 17.8 2.6 

### ' .02 ' 24 3 ' 14.'09 1:45 22' 27.60 

# zs -0 .13 4.4 192 1.4 0.92 

### i u 4
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# "' lnvald data 18.4 

### 2.0 0 .S 1 11 7 Z 2 17.8 2.6 1.01 ' 25 3. '14:08 2:00 

### 222 V.Sl 25
-0.13 30 19.2 1.4 0 .903 110 3 .0 1 9.0 1.6 0.76 110 fnv aJd dal a 18.4 

### 2.0 0 .83 116 2 .0 17.8 26 1.01 , N 3.'1 4':082 : 15 223 27 .S1 25 

### -o.r a 43 19.2 1.4 0.97 

# H'. 3
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### 20 0 .83 11 6 22 11.8 2.6 1.03 124 3.'1 4,032:30 224 27 .S 1 25 -0.1 3 4.5 192 1.4 0.90 

### ' 09 4 .0 1 9.0 1.6 0.73 110 f nva:id dat a. 18.4 

### 2.0 0 .84 11 6 Z3 17.8 2.8 1.03 ' 24 3.' 14.'092;45 225 27 .S 1 25 -0.13 53 192 1.4 0.66 

# " ' 4
.7 1 9
. 0 1.6 0 .88 

# ", I nvaXl dala '8.4 

### 20 083 11 8 2.4 11.8 2.6 1.02 ' 24 31 1 "'093 :00 228 27 .S 1 25 -0.' 3 52 19 .2 1.4 0 .90 110 4 .7 1 9.0 1 ,6 083 

# '" I nva!Kl data 18.4 

### 2.0 0.83 116 25 11.8 2.6 

### '.02 ' 23 :1' 1 4.083 ' 15 227 27
. 8 1 25 -0. 13 5.4 19.2 1.4 O .SoB 110 4 .9 1 9.1 1.5 0 .89 110 In....alid dal a 18.4 

### 2.0 0 .83 Tl6 26 17.8 2 .6 1.03 123 TOA5 TI.'.: ESTAMP

TS 3.'13"-0'; 8:00 3.'13,:C38:15 3.'11-'C88:30 3.'13,:C88:45 3.'11-CB9:OO 3,' 11-'059 : 1 5 3,' 1 3,,08 9 :30 3.' 13108 9 :45 3.'1 3/0 810 : 00 3,' I :WS IO
. 15 3,1 1 3JQ8 10 :30 3,' l lf08 10 :45 3.' 1 3108 11-:C() 3/1 3100 1 1:1 5 3,' 1 :11(.'6 11 :30 3,' 130'06 11 :45 3,' 1 3108 12 :0) 3,' , :1108 12 : 1 5 31 1:1<061 2 :30 3 ' 1 l108 1 2"45 3,; , 3106 1 3 : I)J 3!1 3/0S 1 3 : 15 3.'1:1109 13 : :;0 3113106 13:45 3,' 13/CS 14 :00 3,' 1 310814:15 31 1:11 08 14 :30 3.'11-08**t~:4.5** 3.'1 3108 1 5:00 3.'1 310615 : 1 5 3il l1OB 15 :30 3'1 3Kl615:45 3,'1 310916 :00 3.'1 3108 16:15 3iI3.09 16:30 3i13':09 16:45 3.'11-'0817:00 3, 113,0917:15 3,'13'08 17 :30 3,'13, 08 17:45 3 1 11-'0918:00 3113108 18 : 15 

### 311 3100 18 : 30 3ill'0819:00 .],:, 31 08 19 : 1 5 3.'13/08 1 9:30 3,'1 31 08 19:45 3.'13IC820:00 3.' 1 31C820; 15 Jl l 31C820:30**3I 3.'C9~** **(): 45**  :1'I 1-

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# 20' 2C' 210 211 212 

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### 19
. 0 1,6 1.02 11 0 I nvalid data 18
. 5 2
.0 0
.85 11 5 3
.3 

### 17
.B 2.8 1. 04 1 22 27
. 88 1 9 -0. 1 6 6 . 7 19
.2 1.4 0
. 90 I C3 5
. 8 

### 19
. 0 1
. 6 I
.e.: no invalid data 19
. 9 0.7 0. 85 116 1.8 

### 17
. B 2.8 1. 05 12 1 27.8 9 1 9 -0.1 6 7
.3 19
.2 1.4 0. 95 109 6 .2 19
. 0 1.8 1
.04 11 0 

### i nvalid d::l.I a 18
. 5 2
.0 0
. 85 11 7 3
.2 17
. B 2
. 4 1.00 122 27 .90 19 ·0 .17 7
.0 19
.2 1.4 0.98 l c a 6 .0 

### '9
. 0 1.8 0. 72 I C g ffla; :d dal a 18
. 5 2
.0 0
. 87 115 2
.7 

### 11
. 8 2.8 1. 04 122 27 .91 19 ·0. 17 7
.2 19
.2 1.4 0. 98 107 6 .4 

### 19
. 0 t.8 0.73 l C9 InvaIid dara - 18.5 

### 2, 0 0
. 87 11 5 3
.0 118 2.6 1. 04 J2 1 27
.9 1 19 --0
. 17 6 . 8 19
.2 f.4 0. 9 S 107 6 . 5 

### 19
. 0 1
. 6 0.73 109 tnva.'id dala 

### 18.5 2.0 0. 87 11 4 3
.6 17
. g 2
.S 1. 0 5**~** 27.9 1 1 8 ·0
. 17 6 . 8 19
.2 1.4 0
. 97 10 7 6 . 3 

### 19
. 0 1.6 0.7 9 109 Invaiddata 

### 18.5 2.0 0. 87 11 5 3
. 8 17.9 2.5 1. 04 12 1 27.92 1 8 -0
. 17 6 .3 19.2 1.4 0.95 106 5
. 8 

### 19
. 0 1.8 0. 76 109 In vc6::l dala ,as 

### 2
.0 0. 87 115 27.92 18

-0
. 17 6,4 19
.2 1.4 0.96 100 5.8 

### 19.0 1.6 0
. 75 l C9 Invaid data 18.5 

### 2.0 o .ea 114 27.92 19 -0
. 17 6 . 5 19.2 1.4 0.97 10 7 5.8 

### 19
. 0 1.6 0.80 lC9 Invafid dala 18.5 

### 2
.0 0.87 lIS 27.93 19 -0
. 17 6 .3 19.2 1.4 0.93 105 5. 5 

### 19
. 0 1.8 0
.79 109 In valid data 18.5 

### 2
. 0 0.8 7 lIS 27.93 20 -0.1 7 6 . 8 19.2 1.4 0.97 )07 6.1 

### 19
. 0 1.6 0.81 109 lnvaSd dala 18
.5 

### 2
.0 0
. 86 115 27.93 19 -0
. 17 7
. 0 19.2 1.4 0.95 106 5
. 9 

### 19
. 0 1.6 0.72 109 I nvdki d3ta 18
. 5 

### 2
.0 0.86 115 27.93 20 -0
. 17 7
.3 19.2 1.4 107 5. 9 

### 19.0 1.6 0.58 109 i nv ztld data 18.5 

### 2
.0 0. 85 115 27.94 19

-0
. 1 6 6 . 1 19.2 1.4 

### 109 5
. 0 

### 19
. 0 1.6 0.66 109 Invalid dab. 18.5 

### 2
. 0 0
. 86 115**27.~** 21 -0
. 16 5
.4 19.2 1.4 109
.. . 4 

### 19
. 0 1.6 0.81 109 I rrva5d. dat3 18.5 

### 2.0 0.85 liS 27.94 2 1 -0.16 5
.7 19.2 1.4 \08
... 5 19.0 1
. 6 0.79 109 t nvaid dab. 18
. 5 

### 2
.0 0
. 84 116 27.94 20 -0. 16 5. 0 19
.2 1.4 10 8 3 .9 

### 19.0 1
. 6 0.75 109 t nvaid d.:ata 18
. 5 

### 2.0 0
. 83 115 27
.94 2 1 -0. 16 5
. 1 19.2 1.4 109 4 .1 

### 19
.0 1.6 0
. 72 109 ( nvaid dab. 18
. 5 

### 2.0 0 .8 1 116 27. 94 20 .{l. 16 3
.6 19
. 2 1.4 , ea 2
.9 

### 19
.0 1
. 8 0. 72 109 Irwa! ld dala f8
. 5 

### 2
.0 0.33 115 27
.9<0 2 1 .{l
. I S 4
.7 19
.2 1.4 t 07 3.5 

### 19.0 1
. 8 0.73 lC3 (n ...aid data 18
. 5 

### 2.0 0
. 85 1 15 27
.95 22 .{). t5 5 ,4 19
. 2 f
. 4 107 4
. 1 

### 19
. 0 r . 6 

## o.n 10 9**Inv~d al** **a** 18.5 

### 2
.0 0
. 84 1 15 27
.95 22 ·0. 15 5
.3 19
.2 1.4 1 08 4
. 1 

### 19
. 0 1
. 6 0. 73 t C3 

### Ifwdd dal a 18.5 

### 2.0 O.e.; 1 15 27
. 9 5 22 -0
. 15 

### " 7 '9.2 

### t.4 107 3
.7 

### 19
. 0 1
. 8 0 .80 l C3 Inv8I: d dal a 18
. 5 

### 2.0 0
. 84 1I S 27
. 95 23 · 0 .1 5 4
.5 '9.2 1.4 107 3
. 5 

### 19
. 0 f
. 8 0. 96 10 3 InvaIiddala 18
.5 

### 2.0 0
.85 115 27
. 96 23 -0
. 15 5
.3 19
. 2 1.4 Ice 

### "
.2 19
. 0 1.8 1.07 l C g Inva:. d dal a. 

### 'S
.5 2
.0 0
.84 11 5 27
. 97 23

-0 .1 5 5
. 0 19
.2 1.4 l C9 3
. 9 

### 19
. 0 1
. 6 1. 16 l C3 Invalid data. 

### 1S
. 5 2.0 0
. 8 1 1 15 27.97 2 5 -0
. 14 5
.0 19.2 7.4 leS 3
. 9 

### 19
. 0 1.6 1. 23 I Cg Invaki dala 18.5 

### 2
. 0 0
. 82 116 27.97 27 ..0 .1 -' 4
. 6 19.2 1.4 109 3.5 

### 19
. 0 1
. 6 1.28 IC9 

### Invalid dlIa 18.5 

### 2.0 0 .7 9 1 16 27
. 98 27 -0.1 -' 4
.3 19.2 1.4 108 3.2 

### 19
. 0 1
. 6 1
.24 109**d3Ia** 18
.5 

### 2
.0 0
.8 1 115 27 .98 28 -0 .1 ':' 4
.5 19
. 2 f.4 107 3.4 

### 19
. 0 1.6**~** ' 0 3 Inv;iid dala 18.5 

### 2
.0 0. 82 11 5 27 .98 3 1 -0
. 1 -' 5
.9 19.2 1.4 lCS -'
. 5 

### 19
. 0 1
. 6 0.94 109 I nvalid data 18.5 

### 2, 0 0
. 80 115 27
.99 2<J -0
. 1-' 5
. 5 19.2 1.4 107 4
. 5 

### 19 , 0 1.6 O.ro 109 I nvc'l!'icl dala 18
. 5 

### 2
.0 0
. 81 115**27 .~**  3 1 -0
. 1 ':' 6 .2 19
. 2 1.4 109 5.0 

### 19
. 0 1
. 6 0 .74 109 I nvo:Dd data 18.5 

### 2
. 0 0
.79 lIS 27. 99 32 -0
. 14 6 .2 19
.2 1.4 1 1 1 4 .7 

### 19
. 0 1.6 o .eo 1 10 ( nvaid dolta 18.5 

### 2
.0 0.78 n6 2-8.00 32 -0
. 14 5
.9 19.5 1.3 11 0 4. 6 

### 19 , 0 1.6**o.~** 110 ( nvaid data 18.5 

### 2.0 0. 7 9 117 28.00 3 2

-0
. 14 6. 9 19.5 1.3 110 5. 2 

### 19.0 1.6 0.74 110 I nva'iddala 

### 1S
. 5 2
.0 0.00 116 28.01 30 -0
. 14 8
.2 19.5 1.3 0.93 112 6.2 

### 19
. 0 1.6 0.71 110 I nvaid d3ta. 18
. 5 

### 2 ,0 0.8 1 116 2.8.01 29 -0
. 14 7
. 1 1 9 ,4 1.3 0.87 111 5. 4 

### 19
.0 1.6 0.69 110 Irwalid data 18
. 5 

### 2.0 08 1 116 23.02 26 -0
. 14 6 . 1 '9,4 1.3 0.94 11' 4
. 7 19
.0 1.6 0.71 110 !nvakl dab. 18
. 5 

### 2
. 0 0
. 82 116 29
. 02 24 -0
. 15 6.6 1 9 "; '.3 0.93 110 5.1 

### 19
. 0 1.6 0
.78 110 l rr ·: .:lid data 18
. 5 

### 2 , 0 0 .53 116 28.03 23 -0
. 1 5 6 .5 19
. 5 1.3 0.94 lC 9 5 .0 

### 19.0 1.6 0
.78 110 {nvaid data 18.5 

### 2 ,0 0
. S3 "6 26.C4 22 -0
. '5 6 .5 ' 9 .4 1.4 0.94 

### 103 4 .9 

### 19
. 0 1.8 0.74 110 I nvakl data. 18.5 

### 2 , 0 0
. 53 116 26
. 05 22 · 0
. 15 6,4 19,4 1.4 0
. 95 l Ca 4 .9 

### 19
. 0 1.6 0.73 110 I nvalid dala 18
. 6 

### 2.0 0
. 85 116

· 0
. 1 6 6 .2 1 9.5 1.3 0. 95 l ea 4
. 8 

### 19
. 0 1.6 0. 83 110 !nvaid dab 18
. 5 

### 2
.0 085 116 -0
. 1 6 ·0
. 1 6

· 0. 16 ·0
. 17 ·0. 17 

### ·O. p -0
. )7 -0
. 17
-0
. 12 5
.4 

### 5 .• 5
.5 2. 3 1. 3 

### 0. 5 0
.2 4
.3
-0
.3 19.5 19
. 8 20
. 1 20
. 2 20
. 3 20
.2 14
. 6 1 3
. 3
20.• 1 .3 1.0 0 .' 

### 0
. 5 0 .
.. 0 .5 0. 1 0. 7
0 .4 0. 99 0. 99 0.91 0. 91 0. 91 0. 93 -0.00 -0
.00
0. 64 l C8 1 08 112 112 112 11 0 

# 7'



# ... '.4 5
.2 5.4 

### 2
.5 1. 5 0. 7 0. 1 0.,
0.0 

### 19.0 19
. 0 19
. 0 19
. 0 19
. 0 1 9
. 0 19
. 0 19
. 0 19
. 0 19.0 

### 19
. 0 

# f.' f.O f • • 

# f
.' f
.•



### ..0 

# f
.' f

_ O 

# f.' f.' f.O 0. 93**o.~** O.SS 0
.84 0. 62 0. 97 0. 29 0
.27 0
.06 0. 14 0. 14 ' 10 I nvaid 

### data 18.5 

### 2 ,0 0.S7 1 '5 

# '" l C8 108 l C8 10 7 86 

# n 66 

## sa 

# ..

P;}Jt!5 I nvaid d.:at3. 18, 5 

### 2
.0 0
. 66 il2 ( nvaid data. 18
. 5 

### 2
.0 0.8 1 " 3 Irwaid dal3 18.5 

### 2.0 0
. 82 1 1 3 I nvald dafa 

### 1S
. 5 2 ,0 0
. 82 11 4 Invaid data 

### 1S.5 2.0 0
. 84 113 I nvaid d3ta. 18
. 5 

### 2
.0 O
. IS l O S Invaid dala 

### IS
. 5 2.0 0
. 15 98 Invaid'data 18.5 

### 2. 0 0.1 6 83 Inv<lid data 

### 1 1.7 1.9 O
. s.:: 88 I nvald data. 17
. 7 f
. 9 0 .62 99 3 .2 3
.2 3.1 3.1 

### 3.5 3.3 3.3 

# 2. 2.3 2.4 2.1 2.1 1.' 2.0 2.2 2.2 21 2 .1 2.3 2 1 2
. 1 1. 9 1. 9 1. , 2.2 

### 2 ' 2 .• 2
.2 2
. 1 

### 2.' 3.0 2.6 2.3 

### 2.5 2.' 2.5 

### 2.5 2.6 29 5.6



# . 0 3
. ' 

### 3.a 1
.2 -0 .1 -0
.2 -0
.2 -0 .1 -0 .2 17.9 17.9 17.9 17
.9 17. 9 17. 9 17.9 17.9 17.9 17.9 17.9 18.0 17. 17
.9 17 .9 l S.0 1 8.0 17.9
' 8.0 17
. 9 18
.0



## . ao 1 8
. 0 18
. 0 1 8
.0 1 8 .0 

## l a o 17.9 17.9 17.9 17
. 9 17.9 17.9 17.9 

### 11.9 11.9 11.9 11.9 11.9 17.9 

### 11.9 17.9 17.9 

### 11.9 17.9 17.9 17. 9 f&8 16
. 8 

### 2.5 2
. 5 2
. 5 2.6 

### 25 

### 26 2
. 5 2. 5 2.' 2
. 5 2
. 5 2
. 5 2
. 5 2
. 5 2
. 5 2
. 5 2
. 5 2
.5 2S 2.S 2
.5 

### 2
.' 2
. S 

### 2
.5 2 .S 

### 2. ' 2
. ' 

# 2
. ' 2
. 5 2
.5 2.5 25 2
.5 2.5 2.5 2.5 2.5 25 2.5 2
. 5 25 

### 2.5 2
.5 2.5 2
.5 25 2
. 5 2
. 5 

## 2 5 1. 05
' .05 1 .05 

### 1. 05 1. 05 

# I. ""

'
.02 1
. 03 

# ,,"" 1
.00 1
.0 1 1. 0 1 1.03 

### I
.e.; 1
.02 1
. 02 1
. C

':' I.C4 

### 1. 03 1 .02 

### 1. 02 1.00 1. 0 1 1
.02 

### 1
.02 1
.00**9~** 0
. 99 1.0 1 1.0 1 1. 0 1 1 02 1. 0 1 1. 02 1
. 03 1.03 1
.03 1
.03 1
.0 5 1
.03 0
.95 

### 0
.% O. g.s 

## 0
." 0
. 22 0
. 22 0
. 23 -0
. 50 -O
. SO . 21 12 1 121 12 1 122 121 

# '" ' " 123 123 123 124 124 1 23 1 23 1 23 1 23 1 23 1 22 1 23 

# "
. '" 

# . ,. 1 22 123 122 121 123 12-0 123 1 23 

# '" 124 

# ". 1 23 

# ". 124 

### 123 1 22


### " 7 

# ". 1 19 120 

# ". '" 84 

### 90 92 

# " Com ;r, eo (s

System 

### Bias Drift ChecX

15-t.1L ,RfCOfdod Data. 

### ts-moutc avur ag.-s 

# I STACK A- inputs STACK 

### 6-- Inputs STACK C- inpuls STACK 

### 0- inputs TO A5 N O)! G

EM':: GA 100J 4759 =ll0:<J.S:d.08**~o15 TI** **~/ EST** **p.,:** RECORD arP rd$.SJuTmp_F ..A15 taticP**02 vg** **(1 02** **_A~1 }~** **(1 ,jrFJow1** **V'( Tmp** **_F** _Ay302_Avg (1**02_Avg(2»)Q2_Avg (2,jrAow2~v.TIT'.p_F_1.**  

# = ;;0(1' VQ 

## ::A vrr"", V302..Avg (1**02~ \'g** **(4 )::02_AY9(4.irAow4** **_1.v:k:Tmp_F** _Avg (4) 

### T S RN llHQ 

### Ceg_ n l;.2 0 

### ppm C,., Prcnt Dry PClltOry**H20** 

### Ceg _ ppmC,., Pr<:ntOry P.;ntOry**~ti20** 

### Dog_



### .... C,., P= <Cty 

### P<ntO<y 

### ""20 CooF ppmC<y PrctllDry PcntOfy <>H 2O 

### CegF Avg AV9 

### A'" A "II A"" A"" A "" A "II AVQ A,g A,g A\lg 

### A"" A A AVQ A,g A"II A,g A ""**Com "T:~** **ls** 306 2a.55 23 -009 -0.3 20
. ' 0 .' 0 .65 90 0.0 19.0 

# I .' 0 .55 90 

# "'''''- 17.7 1.' 0.57 a. -0 ,2 16.8 2.S 0 .45
. S 307 2a.56 23 -0
. 13 

### , .t S
. 3 

## a.' 0
. ... .2 14
. 3 19 .0 

# I .' 0.40 90 Invalid da ta 17.7 1.' 0.31 90 1.1 16.8 2.S 0.7 3
. S 30a 2a.56 21 -0. 15 14
.8 11.0 0 2 0
. ... 92 33 .7 19.0 

# I .' 0.33 90 In valid da ta 17 ,7 

# I.' 0.33 

# •• 1 5

_ 2 16.8 2.S 0. 73 

## se 309 2a .56 

### 21 -0
. '6 7 .S 1 U J 2.3 0
. 65 92 7 .' '9.0 

# I.' 0 .33 90 lnvatid dal.3 17 ,7 

## I.' 0,32 90 7. 16.8 2.' 0.74 .S 310 28 .56 '0 · 0. ' 6 ' .4 '
.0 O S 0 .62 93 -02 19.0 

### I.' 0 27 91 Inva/id dal a 17 ,7 

# I.' 0.33 

# •• -0 .2 16 .8 

## 2.' 0.73 

### 95 NlaJ.yz er CalibrabOn 3 11 " .57 2' -0 .17 03 15 .3 .4 0.6 1 95 1.0 19.0 

# I .' 0 ,21 93 

# """"' ''''' J7 ,7 

### I.' 0.32 93 -0 _2 16.8 2.S 0.72 

### 97 3. 2 ,. 57 

# " -0
. 17 -0 .2 19 .9 0.' 0
.5 9 

### se -0. 2 19.0 

# I .' 0.17 96 InvaIld daLt 1 7.7 

### I.' 0.33 96 I .S 18.8 

## 2.' 0.69 100 3.3 ".57 

### t s -e . 17 -0.3 1 9.9 O' 0 .59 

## s s
-0 .2 19.0 

# I .' 0 .0 1 93 I nvaid d ata 17 .7 

# I.' 0.39 ' 7 -0
. 1 16.8 

## 2.' 0 .70 ' 0 ' 314 " .57 . 5 -0
. 1 7 -0 .3 1 9 .9 O' 10 1 -0 .2 19 .0 

# I .' 0 .23 93 l rwaid dala 17 .7 

### I.' 0. 57 

## sa · 0 .' 16.8 2.S 0.69 

### . 02 315 " .57 17 .Q
. 18 -03 20
. 0 O.S 

## o .n 99 -D.2 190 

# I .' 0 .36 

## ss lnvaid d ala 17.7 

# I.' 0.75 ' 7 -0. ' 16.8 2.S 095
. 0. 3 16 " .57 17 -0. 10 -0 2 20
. 1 O.S 0
. 83 97 -0. 1 19.0 

# I .' 0. 3 1 

# ... I nvaid data 1 7.7 

### I., 08 1
. 7

-0
. 1 16.8 2.S 0 ." 

### . 02 3 17 " .57 17 -0
.02 -D. 2 20
.0 O
. S 0 .84 95 -0
. 1 19 .0 

# I .' 0 .47 94 lnvaI: ::ldat a 1 7.7 

# I .' 0 .7 9 

### 98

-0 .1 16.8 2 .S 0 .94
. 03 318 28. 57 1 5 · 0.18 -0.3 

## zo.o O. S 0. 83 .7 

## - o.i 19 .0 1.' 0. 32 94 InvaIid dafa Fl.7 

# I .' 0.40 

## se -0
. 1 16.8 

## 2 .' 0. 93 ' 03 

# 31 ' 28 .56 

## r s · 0.1 9 -0.3 2. 0 ,0 O. S 0
. 83 98 -0. 1 19.0 

# I .' 0
.40 96 

### """"' data 17 .7 

# I .' 0.6 9 

# ss -01**1~8** 2.S**.~** . 03 320 28.55 '5 -0.1 9

-0.2**~O** O
. S 0. 84 96 -02 1 9.0 

# I.' OA2 .5 

# """' 

# .... ir.r 

# I.' 0.8 2 ' 6 

### ·0. 2 16.8 2.' O. !l3 1 04 321 28.54 

### 15 · 0
. 1 9 -0.2 :20. 0 O.S 0 .53 97 -0.2 19 .0 

# I .' 0. 43 96 InvaIid d .:1J !,l. 17.7 

# I.' 0.83 

## ss -0 .2 

### 16.8 2.S 0. 93 100 322 2a.54 

### 15 -0 .19 ·0.3 20.0 O.S 0
. 85 .7 -02 19.0 1
. • 0 .43 94 lnvalid dal a 17 .7 

# I.' 0.84 .7 -0. 2 16.8 2.' 0 .96 

### \02 323 2a,53 

### 15 · 0.19 -0.3 2.0.0 O.S 

## o.ss 95 -0.2 19.0 

# 1.. 0.42 

# .. in",atd dala 

### 17 .7 

# I.' 0.84 96 -0 .2 16.8 2.S 0.94 .00 324 20.53 

### 15 -0 .19 -0.3 2Cl.0 0 .4 0.82 96 -0.2 19 .0 

# I.' 0.42 94 

### I nva:idda t.:1 17.7 

# I.' 0.84 

## ss · 0.2 16.8 2.S 0 .94 \ 0
. 325 

## zs.sa 15 -0
. 19 -0.2 20.0 0. 4 0
.53 95 -0.2 '9.0 1.' 0.43 94 I nva:.d data 17.7 

### I.' 0.84
. 7 · 0.2 16.8 2.S 0 .94 .0
. 326 2a.53 

### 15 .Q
. ,9 -0.2 2J.O 0. 4 0 .53 

## se -0.2 19.0 

# I.' 0.42 '5 I rwa:fd data 17.7 

### I.' 0.84 .8 -0
. ' 10.8 

# 2.' 0 .901- 

### . 02 327 Za.52 

### 15 -020 -0 .3 20 .0 O .S 082 96 -0 ,2 19.0 

# I .' 0.41 95 lnv ,fid 

### eata 17 .7 

# I .' 0.83 90 ·0 ,1 16.8 

## 2.' 0.9..
. 03 328 2:3 .52 

### 15 .Q.19 -0 .3 23 .0 0
.4 0. 53 96 -0 .2 19.0 

# I.' 0. 42 95 

### I nvaJd data 17.7 

# I.' 0.83 .8 -0
.2 16.8 2.S 0.9..
. 03 329 2a .52 ' S -0 .19 -0.3 23 .0 0
. 4 0. 53 

## ss -0 2 19 ,0 

# I .' 0. 43 95 I nv.:Ud daia 17,7 

# I .' 0.84 

## ss -0 2 16.8 2.S 0.9.. ' 03 330 2 <352 

### rs -0 .19 -0
. 3 23.0 05 0 8 1 97 -0. 2 19 .0 

# I .' 0.42 96 

# """"' ''''' 17.7 

# I.' 0 .82 

## sa -0.2 16.8 2.S 0
.94 103 33
. 

### 2a .53 

# • • .0 .19 "
. 3 23 .0 0. 5 0. 60 SO -0 .2 19.0 

# I .' 0.4 1 <6 Inv aid 

### d:da 17 .7 

# I .' 0. 81 

## sa -02 16.8 2.S 0.92 

### ' 04 332 28.52 t .Q
. 1 9 -0 .3 19
. 9 0. 5 0
. 81 98 -0 .2 19 .0 

# I .' 0
.4 1 <6 r nvaid. daIa 

### 17 .7 

# I.' 0. 83 9. -0. '**1~. ~.S**  0 .92
. 04 333 205 1 

### 17 ·0
. 19 -0 .3 1 9. 9 0
.5 0
. 81 93
-02 19 .0 

# 1.' 0. 41 97 [nv aid data 17.7 

# I .' 0 .8 1 

### sa -0 .' 16 .8 2 .S 092 

### . 04 334 2:3.52 17 .Q .1 9 -0. 3 19 .9 0 5 0 .8 1 99 ·02 19.0 

# I .' 0 .40 97**lnv aid**  

### 17.7 

# I .' 0 .78 '00 -0 .1 16.8 2 .S 0 .' i2 

### re s 33 S 

## "'.52 1 8 .0 .18 -0.3 1 9.9 O.S 0
. '" 

### 98

-0.2 19.0 

# I .' 0 .J1 SO Inv dd d ata fl.7 

# I .' 060 

# r eo -0
. ' 16 .8 2.S 0. 9 1 

### re s 336 

## " .52 

# •• -D.18 -0. 2 19 .8 0
.5 0 30 ' 00 

## - o.t 19 .0 

# I .' O A" .9 

### I nvakI data 17.7 

# 1.. 0 .79 ' 0' -0
. '**1~8** 2 .S 0 .9 1 

### res 337 28 _51 

# ts -0. 17 -0.3 19 .8 0
.5 0 .79 '00 -0. 1 19 .0 

# I .' 0.3 9 

## so 

# """' '''''' 17.7 1.' 0.79 ' 01 -0 .1**I~'** 

## 2 .' 0 .92 1 06 336 28.50 

# ts · 0. 17 -0.2 19.8 0
.5 0.79 101 -0.1 19 .0 

# I .' 0 .39 .00 rnafd d a ta 

### 17 ,7 

# I.' O.7a 

### ' 02 -0
. \ 16.8 2.' 0
.92 1 06 33' 28.50 

# • • -0. 17 -0.2 19.8 0 .5 0. 78 .03 -0.1 19 .0 

# I .' 0 .39 .00 In valo

d dal a 17.7 

# I.' 0 .78 

### '02 -0
. 1 16.8 2.5 0.89 1 07 340 28.49 

# • • · 0
. 17 -0.2 19.8 0 .5 0 .78 102 -0.1 19.0 

# I .' 0.39 10. IrNatd d ata 17 .7 

# I.' o.n '02 0.0 16.8 2.S 08 9 107 34' 23.48 

# , . -0. 17 ·02 19.7 0. 5 

## o .n 105 -0.' 19.0 

# I.' 0.36 102 Inv atlddal a 17,7 

# I.' 0.76 \03 0.0 16.8 2.S 0 .87
. 05 342 2:3.47 20 -0. '7 -0.' 19.7 0 .5 0
.76 "5 0.0 19.0 

# I
.• 0.36 102 In\ 'alid dat<1 ,7,7 

# I.' 0.76 \ 04 0. \ 16.8 2.S 0.8 7 . 09 343 23.47 20 

### -0. '7 0.0 19.7 0
.5 0
.76 105 0.0 19.0 

# I.' 0.37 103 

# """' 

# .... 17,7 

# I.' 0.75 '04 0. ' 16.8 2.S 0.8 7 1 09 344 28 

## .ae 

# , . -0
. 17 -0.' 19 .7 0
. 5 0 .74- .07 0 .0 19 .0 

# I .' 0 .37 104 

### In vaSddat a 17,7 

## I.' 0.74 lOS 

## a.' 16.8 2.S 0." .09 345 28
.ae 

## ao -0. 17 0.0 1 9.7 0 5 0
.7 5
. 04 0.0 19.0 

# I .' 0.3 7 104 I nva'Id 

### data 17.7 

### I.' 0.74 lOS 0.2 16.8 2.' O. BS 11 0 346 29 .47 20 .Q., 7 0 .0 1 9 .7 0. 5 0. 7 5 107 0.1 19 .0 

# I .' 0 .37 ' 04 I nwid 

### d.3la 17.7 

# I.' 0. 74 1 05 0 .2 16.8 

## 2.' 0 ." 11 0 34 7 ". 46 

# , 0 -0 .17 0 .0 19 .7 0
. 7 0
. 74 

# .06 0 .1 19 .0 

# I .' 0 .2-3 'OS l r.v.ud 

### data 17.7 

# I.' 0.7 4 

### ' CO 0 .2 16.8 2.S 0 .B 7 .11 :J.l8 28
.46 2 1 -0 .1 7 0
. ' 19 .6 0
.7 0 .74 t 07 O .t 19 .0 

# I .' 0.36 

### r e s l nvaid data 17.7 

# I.' 0 .7 3 1 CoS 0 3 16 .8 2 .S 065 11. 

### 34
. 26.4 7 20 .Q.1 6 0 .0 1 9.7 0
.7 0
.73 107 0
. 1 19 .0 

# I.' 0. 36 l OS If'lllakf data 17.7 

# I.' 0 .67 '06 0
. 3 16.8 2 .S 0.65 11. 

### 350 28
.ae 

### 21 -0
. 16 0
. 1 19.7 0 .7 0 .74 1 06 0
. 1 19 .0 

# I .' 0 .36 ' OS I rw

Uddata 17.7 

# I .' 0
. 46 

### res 0. 3**I~'** 2.S 085 11
. 351 28 .49 

### 21 · 0.16 0. 1 19
. 6 0
.7 0 .72 l ea 0. \ 19 .0 

# I .' 0. 36 1 05 

### lnvDd oala 17 .7 

# I .' 0. 46 107 0. 2**1~8** 2 .S 0 ." 11 2 352 28 .47 

### 21 -0 .16 0.0 19 .5 

## a .' 0 .73 

### 'CO 0. 1 19 .0 

# I .' 0. 37 1 05 I nvaliddala 17.7 

# I.' 0 .47 107 0 .2 

# IdB 2.S 0. " 11 2 3S3 2i1.4.6 

### 21 -0 .16 0 ,5 1 9.3 1.0 0 .73 

# .03 0.3 19 .0 

# I .' 0. 36 . 04 nvalid d.1 la '7.7 

# I.' 0 .47 10 7 0 .3**1~8** 2.S 0 .89 11 2 3S4 

## za.as 22 -0 , 16 1.0 19 .4 1.1 0 .75 11. 0 .6 19.0 

## i.e 0.3 7 105 

### Invalid data ".7 

# I.' 0 ..:.7 

### .09 O.S 16.8 

# 2.' 0. " 11 6 355 2i1.46 22 -0. 16 1.1 19 .5 '
. 0 0.79 .09 0.7 19 .0 

# I.' 0 .39 104 lnV3.'id da la '7,7 

# I.' 0 .46 

### ' 07 0 .7 16.8 

# 2.' 0 92 

# " ' 356 29.45 23 , 0
. 16 '.2 19.5 .0 0 .79 '10 05 19 .0 

# I.' 0,37 105**,),l** 17.7 

# I.' 0 .52 11 0 

## a .' 16_8 2.' 0.92 115 357 26.40 2' -0
. 16 1.7 19.01- 

## ' .1 0 .79 '10 

# ., 19.0 

# I.' 0.68 107 I nvUl cWa 17.7 

## I.' 0.79 11 0 1.2 16.8 

# 2.' a ." 117 359 28.45 

# " -0
. ' 6 2.1 19.5 1. , 0 .86 '09 '.3 19 .0 

# I.' 0.83 107 I nva'id d.:l.ta 

### 17,7 1.' 0 .65 

## u a 1.3 16.8 

## 2.' 0 .99 11 5 359 26.45 2' -0. ' 6 3 1 8
. ' 1.1 0. 84 110 1.6 

### 19 .0 1.' 0.83 '07 I n v

iUd eata 17.7 

### I., 0.85 11. \.4 16.8 2.S 0 .9 7 11
. 360 28.<15 

# " -0
. 15 1.7 19 .6 1. 0 0 .82 110 3 .S 

### 19 .0 1 .' 0.79 

## ice Invalid data 17.7 

### I., 0.81 114 1.3 16.8 2.S 0 ." 

### ' 20 301**28 .~**  

### 2S ·0.1 5 I.' 19 .5 1.1 0 .9 1 .08 '.4 19 ,0 

# . .. 0.89 .08 Inv alld 

### data 17.7 

# I.' 0.B9 113 1
. 3 16.8 2.S 1
.02 

# .19 Sys l iWT'l Bias On! t Check 362 ".44 

### 2S -0 .\5 22 15 ,2 0
. ' 0 .92 108 I.S 19 .0 

### i.e O .BB 108 Irwaid 

### data. 17.7 

### I.' 0 ." 113 3 .3 16.8 2.S 1.0 1 

# " ' 363 ". 43 2. .Q
. 14 3 .3 19 .5 1.1 "'0 '09 2 .3 19 .0 

# I .' 0. 55 10 ' l m aid (jOlta 17.7 1.9 0.8 7 

# ,,':
'
. 8 16.8 2.S 0 .93 

### . 20 364 26
. .:.3 

## zs -0
. 14 3 .0 19 .5 1.1 0. 9 1 ' 09 2.3 19 .0 

# I .' 0 8 7 . ea 

# """"' 

# .... 17.7 

# I .' 0." 11 2 I. ' 16.8 2.S '
. 03 1\8 36S 28.42 2
. -0
. 14 3 .2 1 9.0 0
. ' 055 113 2
. 19.0 

# I .' 0 .82 110 Invali d da ta 17.7 

# I .' 0.82 

# ' " 2S 16.8 2.S 0 .96 

### . 21 355 28 .41 27 ·0. 1 5 22 1 9
. 5 1.1 0. 91 11 1 1.6 19 .0 

### I.' 0 .87 

### rc Inva' d dOlta 1 7.7 

# I.' 0 .87 

# ' " r .5 16.8 2 .S 1.02 . 2 • 367 26 . '; 1 26 ·0
. 14 2 .8 19
.4 1.2 0 .9 1 110 2.2 19 .0 

# I .' 0. 67 . 03 InvaII d oa tt 17.7 

# I.' 0 .55 11 3 1.7 16.8 2 .S 1. 0 2 1 21 36 3 28 .40 27 · 0. 14 3_3 1 9
.4 1.1 0 ." 111 2.. 1 9
. 0 

# I.' 0 .8 9 

### r ca invali d da ta 17.7 

# I .' 0 .84 113 

### I. '**1~8** 2 .S 0
.S9 . 20 36. 28.39 27 -0 .1 4 3 1 19
.4 1.1 0. " 112 2 .' 19 .0 

# I .' 0 .87 11 0 I nvalidda: a 17 .7 

# I.' 0 .84 11 5 

### I. ' 16.8 2.S 0 .99 12 1 370 28 .39 27 -0
. 14 3.S 19 .5 1.1 0 .B2 11 2 2 .7 19 .0 

# I.' 0. 85 110 

### """"' data 17.7 

# I.' 0 .8 5 l1S 2.1 16.8 2 .S 

### I. CO ' 22 371 28 .36 28 -0. 1';' 33 19 .5 1.1 0.9 1 110 2. 7 19 .0 

# I .' 0 8. ICO 

### Invalid data 17.7 

# I.' o.es 11': 2_3**I~'** 2.S 

### 1
.03 12 1 372 2i1.38 

# ,. -0 .14 3.9 19.5 1.0 0. 90 110 3.2 '9 .0 1.' 0.87 11 0 

### Ln validdata 17,7 

# I.' 0. 85 11 4 2.8 16.8 

# 2.' 1
.04 

### \21 373 2i1.36 29 -0 . 13 3. 19 .5 1. 0 0,9 1 '11 32 19.0 

# I.' 0.87 110 lnv a'id da l a 17,7 

# I.' 0.B6 115 2.
. 16.8 2.S 1.03 '22 374 2a.37 

### 2a -0. ' 3 U 19.5 1. 0 0 .90 11' 3.4 19 .0 

# I.' o.as '10 In va1d d.:lta 17,7 

# I.' 0 .05 

# ," 3. 0 16.8 2.S 1.03 12 \ 375 28.37 28 -0. 13 U 19.5 1.1 O. SO 

# "' 3.S 19.0 

# I.' 0.87 110 I nvtUo::f data 17.7 

## I.' 0.80 llS 2 .' 16.8 2.S 1.00 

### .22 3/1 7:08 14 :00 375 28. 37 

# ae -0. 14 '.7 19.5 1.1 0 .9 1 '10 3.8 19.0 

# I .' 0.87 110 !nva'id d,),la 17.7 

# I.' 0.85 l1S 3. ' 18.8 2.S 

### ' .02 .22 3/17 '0814 : 15 

## srt 28 .35 

# ,. -0 , ' " 4.9 19.4 

# . , OBa 

# ' " 3.' 

### 19 .0 1 .• 0.85 110 I nva1d 

### data 17,7 

# I.' 0.B2 

# " ' 29 18.8 2.S 1 .0 2 123 J, ', 7
. ca 1 4:30 378 26
. 35 

# , . -0 .' 3 S.3 1 9.3 ' 2 0 .87 11' 

# , ., 19 .0 1 .' 0 ." 11 ' f nvajd dat a 17.7 

# I.' o.a : 115 2.7 16.8 2.' 1.01
. 2' J, 'l7'CS 1 4 :4 5 379 2a
. 34 28 -0. 1 5 52 19 .3 '3 0 .87 

# ' " '. 0 19.0 

# . .• 0.i13 11 ' f nva"d 

### d.:aLa 17.7 

# I.' O. Bl 11 5 2. S 16.8 2.S 1 ,01 12' 3/ 17 1ca 1 5:00 360 28 .33 

# z e

-0.13 .. . 8 1 9
.2 1.3 0 .89 110 3.6 19 .0 

# I .' 0
. 84 \11 f nvaXj d.:da 17,7 

# I.' o.n 11 5 2 ' 16.8 

## 2.' 0.93 12' 3 .'17,03 15
. 15 36 1 28
. 33 

### 2a -0 .19 .. 9 ,.2 1.2 0 .85 11 0 3 .7 19 ,0 

# I.' 0 .82 110 [ rw'" d ata 17.7 

### I.. 

## o.a r 117 23 16.8 2.S 097 . 25 3/17ica 1 5; 30 3a2 :;:8.32 29 -0
. 19 4 .8 19 .2 1.2 0. 85 11 0 3
.7 18 .9 1. 6 0. 81 110 l nvaid dala 17.7 I.' 0 50 

### 117 22 16 .8 

## 2 .' 0 .97 125 :l' 17iC31 5:45 3S3 2a. 32 

# ., -o rs 48 192 1.2 

## o.es res 3.7 19
. 9 1. 6 0 .112 

# .e , [m aid 

### dab 17.1 

# I .' 0.60 

### 11 0 2. 0 16 ,8 2 .' 0.93 12S

Pol. J .. 6 TOA

5**ST AMP**  TS

3/ 17:08 14 ; 1 5 3i1 7:ca 14 : 30 3! 17

1 C8 1 ';':45 3/17, ca 15:00 3/17

," 03 15.15 3/t 7J

ca 1 5 :30 l ' 17;C3 1 5:45 Rec ordod D ata. 15-mlnIfo avurages 

# I STACK A- inputs 

### STACK 

## So inputs 

### STACK C- inputs 

### STACK D- 

### inputs

# NR**E~.~~ ~H** **T~~; ~=~~~** **~~ vg** **1 ~~~l** **:;OUV g(** **,j rFla.Y1** **Y( mp** **F**_Av302_A'I9!l 02j.'Ig (2)X>2_Avg (2.irA0vr2J\v.Tmp_F_A· .....""""""""'"

# !~;**E~ liQi.102** **-3 ..A;"'** **1 02** **j.vg ~_Avg** **4.iff1ow4_**...dtTmp_F _Avg (4) RN in Hg Deg F n l;,20 ppm O ry PrcntD ry PcntOIy inH20 

### 0 "11 F ppmDry Pr l: ntOry PcntOry

### in**tl2O Dog** **~2: ~**  ppmOfy PrcntOry PentOty i\H2O Oeg 

### F Avg "'\'9 A\ 'g A vg Avg Avg A Yg A vg Avg Avg A vg A "-J A vg Avg Avg Avg Avg Avg



# _ _ a**~ ~**  

# _ u**~** 00 M _**~ ~**  00**~_ ~**  

# u**~** 

### M**~ ~**  

# u**~** 

### % 307 308 3'0 3 11 3'2 3 '3 3 14 3,5 316 3 , 7 3'8 3'9 3>0 32' 322 323 324 325 326 327 328 329 33' 33 2 333 334 33 5 336 337 336 339 34' 342

349 350 

# "' , 352 353 354 355 356 357 358 359

364 365 306 367
370 371 372 373 374 375 376 

### 377 378 379 38J 

# 38' 3a2 3S3 2a.56 23 .(J, 1 3 1.1 5. 3 0 .1 0.64 92 14
.3 19
. 0 1
. 6 0
.4.0 90 

### Invalid data 17.7 1.9 0.31 900 1.1 16
. 8 2.5 0.73**~s** 2a.56 2 1 ·0. 1 5 14
.6 11.0 0
.2 0.64 92 33
. 7 19.0 1
. 6 0 .33 90 In valid dat3 17
. ' 1.9 0.33 91 1 5
. 2 16.8 2.5 0.73 

### SoO 2a
. 56 2 1 -0. , 6 7
. 5 1 1.5J 2
. 3 0.65 92 7
.6 19
. 0 1
. 6 0 .33 90 Invafid dat1l 17
. 7 1.9 0.32 90 7
.6 76.8 2.5 0.74 95 28.56 ZO ·0. 1 6 4.4 4
. 0 0
. 5 0
.62 93 ..0
.2 19
. 0 1.6 0 27 91 Jnvalid d3 1 1l 17
. 7 1.9 0.33 9 1 -0 ,2 16
. 8 2.5 0.73 95 2'B
.57 2 1 -<l.T7 0.3 15
.3 1 .4 0.6 1 95 1
.0 19.0 1,6 0.2 1 93 Invaiddala 17
. ' 1.9 0.32 93 · 0
. 2 

### 16.8 2.5 0.72 97 

### 28 .57 19 ·{:U7 ·0
.2 1 9.9 0.6 0.59 

## sa -0. 2 19.0 1.6 0.17 

### 96 Invalld daJa 17
. 7 1.9 0.33 

### 96 1
.5 

### 16
. 8 2.5 0.8 9 100 

### 28.57 1 9 -0. 17 -0.3 1 9.9 O.S O.SS 9 9 · 0.2 19.0 1, 6 0.0 1**~** I nvaid d.lta f7
. 7 1.9 0.3 9 97 · 0
. 1 

### 16,8 2.5 0. 7 0 10 1 

### 28.57 1 5 ·0. 17 · 0.3 19.9 0.6 O.S S 1 01 -0.2 '9
. 0 1
.6 0.23 1i3 I nvaid daca 17
. 7 1
.9 0.57 98 · 0. 1 

### 16.8 2.5 0.69 102 

### 28.57 17 ·( U S -0.3 20
. 0 0.5 

### O.n 99 ·0.2 19.0 1,8 0.36 

### S6 Invaid dala 

### 17 .1 t.9 0.75 97 -0.1 16
. 8 2.5 

### O
. SS 10 1 

### 28.57 17 -0. 10 -0.2 20. 1 0.5 0.83 97 -0. 1 19
. 0 1
. 8 0.3 1 94**nvaid ~**  

### 17.1 t.9 0
. 8 1 97 ·0,1 16
. 8 2
.5 0.94 102 

### 28.57 17 · 0.02 ·0. 2 20
.0 0.5 0
.94 

### 9S -0.1 

### 19
. 0 1
. 6 0.47 94**~d at** **a** 

### 17. 1 

### 1.9 0.79 

### 98 ·0.1 

### 16
. 8 2
.5 0.94 103 28.57 16 · 0.18 -0.3 ro.O 0.5 0.83 97 ·0. I 19
. 0 1.8 0.32 94 

### kwaIid dala 17
. 1 1
. 9 0.40 liS -0
. 1 

### 16.8 2
. 5 0.93 103 28
. 56 Hi ·0. 19 ..Q.3 2 0
.0 0.5 0.83 98 -0. 1 19. 0 1
. 8 0.40 96 

### Invalid data 

### 17
. 7 1.9 0.69 /jo9 -0
. 1 16.8 

### 2.5 0.93 103 28 .5 5 1 5 -0.19 · 0. 2 ':'0 .0 0. 5 

### 0. 84 96 ..Q. 2 19.0 1
. 6 0. 42. 95 

### 1nvaIid da!a 

### 17.7 1.9 0.8 2 98 

### ·0.2 

### 16
. 8 2.5**0.~3** 104 28.54 I S · 0. 19 -C .2 ::0. 0 0.5 0.63 97 -C.2 19
. 0 1
. 6 0. 43 96 Invalid dOlfa 

### ,7.7 1
. 9 0. 83 99 -0.2 16.8 2.5 0.93 103 2i!.54 1 5 -0. 1 9 ·0.3 20.0 0.5 0.85 97 -C2 

### 19.0 1
. 8 0. 43 9.. Invalid data 17.7 

### '.9 0.84 97 -0.2 

### 16.8 2.5 0.96 102 2i!.53 15 ·0. 1 9 -C.3 20.0 0.5 0.84 95 ·0.2 19.0 1.6 0.42 94 inv.:ttd dala 17
. 7 1.9 0.84 96 -0.2 

### '6.8 2.5 0.94 100 20.53 IS -0. 1 9 -C.3 2Cl.0 0.4 0.82 96 -C.2 19
. 0 1
. 6 0,42 94**n~ dJ.101**  17.7 1.9 0.84 96 ·0.2 t6.8 2.5 0.94 10 1 2i!.53 I S -0. , 9 -0.2 20.0 0. 4 0.83 905 -C.2 

### 19.0 1.6 0.43 94 I nvl.l'id data 

### 17 , 7 f.9 0.84 97 ·0.2 16,8 2.5 0 .94 10 1 2i!. 53 15 -0. 1 9 -C .2 2J.0 0.4 0.83 % -C.2 19
. 0 1
. 8 0
.42 95 I nva1d data 

### 17
. 7 1.9 0.84 98 -0. 1 

### 10.8 2.5 0
. 94 102 2i!.5 2 ' 5 -0
.20 .{l. 3 20 .0 0.5 0
. 82 96 ·0
.2 19.0 

### 1,8 0. 41 95 Lnvald dall.l 

### 17
. 7 1.9 0.83 9il ·0
. 1 1S.8 2.5 0. 94 103 2:3.52 IS -0. 1 9 -C. 3 2:).0 0.4 0.83 96 · 0. 2 19.0 1
.6 0. 42 95 I nvoUd data 

### ,7.7 1.9 0.83 98 -0.2 16.8 2.5 0 .94 103 2a.52 IS -0.19 -C.3 20.0 0.4 0.83 93 .{l
.2 

### 19
. 0 1
.6 0.43 95 I nvl.l.'id dal a 17 , 7 f, 9 0.84 98 -0
.2 16.8 2.5 0
. 94 103 2a.52 16 -0. 1 9 -C.3 20.0 0
. 5 0.S 1 97 -C.2 19
. 0 1
.6 0.42 96 LnvaId dala 

### 17.7 1,9 0. 82 98 -0.2 

### 16
. 8 2.5 0.94 103 2a.53 16 -0
. 19 -0.3 21)
.0 0.5 0.80 S3 -0.2 

### '9.0 1
.6 0.';" 96**In .:Ud** **~** 

### 17
. 7 1
. 9 0. 8 1 9; -0
.2 16.8 2,5 0.92 104 28,52 16 -0. 19

-0.3 19
. 9 0.5 0
. 8 1 9a -0
.2 19
. 0 1
. 8 0
.4 1 

### 96 I nvaid dala 

### f7
. 1 1.9 0.83 9; .{). 1 

### 16.8 

### 2,5 0.91 104 20.5 1 17 -0.19 -0.3 1 9.9 0.5 0.8 1 

## sa

-02 19
. 0 1,6 0.4 1 9 7 [nvald data 

### 17.1 1.9 0.8 1 9; -0
. 1 16
. 8 2
.5 0
.92 104 2:3.52 17 -0.19 -0.3 19
. 9 0.5 0 .8 1 99 ·02 19
. 0 '
. 8 0.40 97 Invaid dllta 

### 17.7 f.9 0
.78 100 -0.1 16
. 8 2
. 5 0.S2 l CS 2a.52 18 -(1.18 -0.3 19.9 0.5 O.SO 9S

-0.2 

### 19
. 0 1
. 6 0.':'1 S9 I nvald data f7.7 1.9 0
. 8,) lev -0 .1 16
. 8 

### 2.5 0.9 1 l C5 28 .5.2 19 -0.18 -0. 2 19 .8 0
.6 0 

## ao 100 -0. I 

### 19
. 0 1
. 6 O A O 99 l nvaid data 

### 17
. 7 1.9 0.79 101 -0.1 16.8 2
. 5 0.9 1 l C5 28. 51 1 9 -0. 17

-0 .3 19 .8 0
.6 0
.79 100 -0. 1 

### 19.0 

### 1.6 0.3 9 99 1nvaid da1& 

### 17.7 f.9 0.79 101 -0.1 

### 16.8 2
. 5 0.92 J 06 28. 50 1 9 ·0. 17 -0.2 19. 8 0. 6 0.79 101

-0. 1 

### 19
. 0 1
. 6 0. 39 100 Invafd data 

### 17,7 1.9 0.78 102 .0.1 16.8 2.5 0.92 106 28.50 1 9 -0. 17 -0.2 19.8 0 .6 0.78 103 -0.1 19
. 0 1
. 8 0 .39 100 Invalddata 

### 17.7 1.9 0.7 8 102 -0.1 16.8 2.5 0.89 107 28.49 1 9 · 0
. 17 -0.2 19.8 0
.6 0 .78 102 -0.1 19.0 1
. 6 0.39 101**ata** 17
. 7 1.9 

## o. n 102 0.0 16.8 2.5 0
. 89 107 28.48 19 .0. 17 -02 19.7 0.6 

## o .n 105 -0.1 19
. 0 1
. 6 0.38 102 In"Iatlddal a 

### 17,7 1.9 0.76 103 0.0 16.8 2.5 0.87 105 2:3.47 20 -0. 17 .{l.1 19.7 0
.6 0 .7 6 105 0.0 

### 19.0 1
. 8 0.38 102**1n\'a6ld~** 17,7 1.9 0.76 104 0. 1 16.8 2.5 0.87 109 28.47 20 -0. 17 0.0 1 9 .7 0. 6 0.76 105 0.0 19
. 0 f
. 6 0.37 103 InvaIid data 

### 17, 7 1.9 0.75 104 0. 1 16.8 2.5 0.S7 109 28 .48 19 .0.17 .{l
. 1 1 9] 0. 6 0.74 107 0 .0 19
. 0 

### 1
. 6 0
. 37 104 Inva'id datl.l 17.7 

### 1.9 0.74 105 0. 1 16.8 2.5 0.86 109 28 .48 ::0 -<l.17 0.0 1 9.7 0. 6 0. 7 5 104 0.0 19
. 0 1.6 0.3 7 104 1 nva5dda1;a 17.7 f.9 0. 74 105 0.2 f8.8 2.5 0.8 5 110 29. 47 20 -0.17 0.0 1 9] 0.6 0.7 5 107 0.1 19
. 0 1,6 0
.37 104 I nvaid aata. 

### f7
. 7 1.9 0. 74 10$ 0.2 16.8 2.5 0.86 11 0 28
.46 

# 'v -0.17 0.0 19.7 0.7 0.7.;. 106 0. 1 

### 19
. 0 1
. 6 0.26 105 

### [1l\'3id cSala. 77.7 1.9 0.7 ';' l eo 0.2 16.8 2.5 0.87 "1 28A6 2 1 -0. 17 0
. 1 1 9
.6 0
. 7 O.N 107 0.1 19
. 0 1.8 0.36 l OS I n'laid data 17
. 7 1.9 0]3 !COS 0
. 3 16
. 8 2
.5 0
. 85 11 1 28 .47 20 .a.t6 0
.0 19.7 0.7 0.73 107 O. I 19
. 0 1
. 8 0
. 36 l OS Im.

- aid data 

### fl
. 7 1.9 0.67 lOS 0.3 16.8 2
.5 0.85 ' " 28.48 21 -0. 16 0. 1 19.7 0.7 0.74 106 0. 1 19
. 0 1
. 8 0
.36 l OS In 'laid data 

### 17
. 1 1
. 9 0.46**C~** 0.3 16.8 25 0.85 I I I 28A9 21 ·0.16 0.1 19. 6 0.7 0.72 l CO 0.1 19
. 0 1
. 8 0.36 106 Invaid O;;&la 

### 17.7 1
. 9 0.046 107 0.2 16.8 2
. 5 0
. 86 11 2 28,47 21 .0
. Hi 0.0 19.5 0.9 0.73 100 0.1 19
. 0 1
. 8 0.37 105 l nval!ddala 17
. 7 1.9 0.47 107 0.2 

### 18.8 25 0.88 11 2 2 a. 46 2 1 -0,16 0
.5 1 9.3 1
.0 0.73 10 3 0.3 

### 19
. 0 1.8 0.36 I OJ lnvaIid da.l a 

### 17
. 7 1.9 0 .47 10 7 0.3 16.8 2.5 0.89 11 2 2a
. 46 22 -0. 1 6 1
.0 1 9. 4 1. 1 0.75 " 1 0. 6 19.0 f.6 0.3 7 105 Vwaid dala 17.7 1.9 0
... 7 109 0.5 16.8 2.5 0.90 116 2a.46 22 .0. 16 1.1 19
.5 1 .0 0.79 109 0.7 19
. 0 1
. 6 0
. 39 104 Inv3.. 'id dala 

### 17,7 1.9 O A 8 107 0.7 16.8 2.5 0.\?2 29.45 23
...CU6 1.2 19. 5 1
.0 0.79 110 0
. 8 f9
. 0 1.6 0
.37 105 Inva!id dl.lla 

### 17,7 1.9 0. 52 

### 110 0.9 16.8 

### 2.5**O.~** 116 28.40 24 .0. 1 6 1.7 19.4 

### U 0 .79 110 19
. 0 1.6 0.68 107 Inva'id dala 

### 17,7 1.9 0. 7 9 1 10 1.2 16.8 

### 2..5**O.~** 117 28.4.5 2':' .0. 16 2.1 19.5 1 .1 0 .86 109 1.3 

### 19
. 0 1,8 0.83 107 I nva:ia dalo. 

### 17,7 1.9 0
.65 112 1 .3 

### 16.8 2.5 0.9-9 11 8 28.45 24 -<l. 16 3
. 1 8.9 1.1 0. 84 110 1.6 19
. 0 1,6 0.83 107 f ny

<Dd dala 

### 17.7 '.9 0.85 111 1 A 16.8 2.5 0.9 7 11 6 28 .45 24 -<l.tS 1.7 19
.6 1. 0 0.82 110 3
.5 19
. 0 1, 6 0
.79 lC8 fnvaiddal3 

### 17.7 1.9 0.81 11 4 1.3 1S.8 2.5 0
. 92 1 20**28 ~**  25 ·0.15 1.9 19.5 1
. 1 0.91 10 8 1.4 19
. 0 1
. 6 0. 89 108 Inv aid daia 

### 17.7 1.9 0.89 

### " 3 1 .3 16.8 2.5 1.02 119 28. 44**5** -0.1 5 2. 2 15
.2 0
.9 0.92 108 1. 5 19
. 0 

### 1.6 

## o . .ss l oa [nvaid dala 

### 17.7 1.9 O .sa " 3 3
.3 16.8 2.5 1.0 1 11 9 29. 43 20 -0. 14 3
.3 lS.S 1.1 

### 0.'10 109 2
.3 19
. 0 1
. 6 0. 86 103 Invaid data 17.7 1..9 0.8 7 1 14 1 .8 16.8 2.5 0.93 120 28.43 26 -o. g 3.0 19. 5 1.1 0.91 1 09 2.3 19
. 0 1. 6 0. a 7 t CO Invaiddala 

### 17.7 1
. 9 0.88 112 1 .9 16.8 2
.5 1 .03 l Ie 28.42 26 .0. 14 3. 2 19.6 0.9 0
.&5 113 2
.6 

### 19
. 0 1
.6 0.82 110 1nvaIdd3la. 

### 17.7 1.9 0.82 114 25 16
. 8 2
. 5 0.90 1 2 1 28 .41 27 ·0. 1 5 22 19.5 1.1 0
. 9 1 II I 1.8 19
. 0 1
. 6 0
. 87 10 InvoI6d d ata 17.7 1.9 0.87 114 1
. 5 16
. 8 2
. 5 1. 02 1 2 1 26 .41 26 ·C.1 4 2
. 8 19
.4 1.2 0.91 lTO 2.2 1 9
. 0 1
. 6 0.87 103 InvaIiddata 

### 17.7 1.9 0.66 t t 3 1.7 16
. 8 2
.5 1 .02 1 2 1 28.40 27 ·0.1 4 3_3 1 9. 4 

### t. I 0.88 111 2.6 

### 19
. 0 1
. 6 0
.6 9 1 C3 InvaEd dal a 

### 17
. 7 1
. 9 0. 84 113 1. 9 16.8 2
.5 0 .$ 9 IN 28.39 27 

### -OJ 4 3
. 1 19.4 1
. 1 O.sa 11 2 2 .4 19
. 0 f , B 0.87 110 I nvalidda! a 17.7 1
. 9 0. 84 11 5 1. 9 16
. 8 

### 2.5 0.99 12 1 28.39 27 -0. 14 3 .5 19.5 1.1 0.82 11 2 2.7 

### 19
. 0 1
. 8 0.85 1 10 

### Invalid data 

### 17.7 1.9 0.8 5 115 2.1 16
. 8 2
. 5 1. 00 122 28
. 38 2 8 -0. 1.. 3.3 19 .5 1.1 0.9 1 110 2 .7 19
. 0 1
.6 08 9 l C9 

### InvaIidctala 

### 17.7 1.9 O.e.g 11':' 2
. 3 

### 16.8 2
. 5 1.03 121 2a.38 2i1 -0. 1';' 3.9 19.5 1. 0 0.90 110 3.2 19
. 0 

### 1.6 0 .87 11 0 

### Illvmiddala 17.7 1.9 0.85 11 4 2.8 16
. 8 25 1.04 121 2i1.38 

### 2"9 -0. 13 3.9 19
.5 1 .0 0.9 1 111 3
. 2 19.0 1
. 6 0.87 110 

### Lnva'id do.ta 

### 17.7 1.9 0.86 115 2.8 16.8 2.5 1.03 122 2a.37 

# z a .0. 13 4.3 19.5 1. 0 0
.90 III 3.4 

### 19
. 0 1.6 0.!!6 110 Inva'id d\).la 17,7 

### ',9 0.65 1 15 3. 0 16.8 2.5 1.03 121 2a.37 28 .0. 13 4.3 19.5 1
. 1 0.90 III 3.5 19.0 1.8 0.87 110 I nva:id do.la 

### 17.7 1.9 0.803 2:3 .3 7 

# za -0. 14 4.7 19.5 1.1 0.9 1 110 3.8 19.0 1, 6 0.87 110 f nvl.l.'id dl.lll.l. 17.7 

### 1.9 0.85 28.35 2a -0.1
.. 4.9 19,4 1
. 1 0.88 I II 3
.9 19
. 0 1.8 0.85 110 I nva.'tddala 

### 17.7 1.9 0.82 23
. 35 a8 -0.13 5
. 3 1 9. 3 1
. 2 0.87 ' I I 4 .1 

### 19
. 0 1.6 0. 84 I II f nvaSdd31 a 17.7 f.9 O
.a l 2a. 34 Zel -0. 1 5 5. 2 1 9.3 1. 3 0.87 111 4.0 19
. 0 1
. 6 0.il3 II I I nv.D:l d.lla 17.7 1.9 0.81 28. 33 

# za ·0.13
.. .8 1 9.2 1.3 0.89 1 10 

### -3.B 19
. 0 1, 6 0. 84 11 1 f nv

aSd data 17.7 

### 1.9 

## o.n 28.33 20 -0.19 ':'
.9 

### 192 1
. 2 0
. 85 1 10 3.7 19
. 0 1
. 6 0.82 11 0 I nvaid dal a 

### 17.7 f
. 9 O.al :;:8,32 

### 2"9 -0
. 19 ';'
. 8 19
.2 1
. 2 0.85 11 0 3.7 18
. 9 1.6 O.al 11 0 Invaid d.lIa 17.7 1.9 0.60 28,32 Z3 ·0
. 1a 4 .8 f 9. 2 f
. 2 

## o.as tOS 3.7 18
. 9 1.6 0 .82 t o; I nvaid 

### d.JIa 17.1 '.9 O.S=) 115 115 11
. 11. 11
. 11
. 117 

# ,,, 11 6 2.9 3. ' 2
. 9 2.7 2.5 

### 2.4 23 22 20 16.8 18.8 IB.8 16.8 16.8 

### lB.8 16
. 8 t6
.8 18
. 8 

### 2.5 2-5 

### 2.5 2.5 2.5 

### 2.5 2.5 2
.5 2
.5 1. 03 1. 02 1.02 1 .0 1 1 .0 1**0.9~** 0
. 97 0.9 7 0.93 

### ' 22 '22 123 

# ,,, ,,, 124 125 125 125R lIfCOf dttd Cata 1 5-rTWllJteaverat;; o!'S 

# I STACK A- inputs STACK 

## B- inputs STACK C- Inputs STACK 

### D- inputs TOA5 ,'\0..**E.·.~S** CA1000 4 789 ::;1000.510.08 TClIb\(j1 5**I~.~ 5TA** **~.~** RECORD i1I'?r t!is _A\ rTrnp_F _AGl<J.tc P_A\'{302_Avg(1 02Jvg (1 ); 02_Avg(1**~rFIow _A** **V( Tmp_F**  _A v302.-M g{1 0 2.-Avg(2) XY.!_AYg(2.irFloY.'2_Av.TITlP_F_Av 

### -"II**):102:'** 

### _ v:i' rnp Y302_Avg(102_A vg (4 }:;02_Avg( 4.irfIow4_Av:lr.Tmp_F_Avg(4 ) TS 

# "f<**~"IHg** 

### Dog F Lr';H 20 ppmDry Pf cmDry PcntOry inH20 

### D og F ppmDry Pr c ntOry P cnlDry n H20 

### DogF ppmOOY. 

## f'1a""'Y ... tOoy 

# """" Oegf ppm Doy PfcnlOry PcntOry inH2Q 

### DogF A \'g A V9 A", A", A", A", A VO A v, A", A v, Avg 

# A' , A A ,g A,g A", A,g A 

### v

# s Com.T.ools 3.'17.'08 1 6:00 3Sl 28 .3 1 

# ze -0 .18 5.2 19.2 1.2 0 ." 10 9 1 8.9 

## r.s 0.83 '08 Invaliddat3. 1 7.7 

# I.' O.Sl 11 5 2 .1 16.8 2.5 1 ,01 

### ' 25 31171

08 16 :15 

### 38S 28 .3 1 30 -0.18 4.7 19.2 1.2 0. " 

# ", 3.' 1 8.9 1. 6 0.83 "0 JnvaIid OOl n 17.7 

# I.' 0 .80 117 1. 8 16.8 2.5 1.0 1 '26 3.'17

/08**~6 30**  366 28.30 33 -0 .18 38 19.2 1.2 0.86 

# ", 30 lS.9 1.6 0.84 

# ", Invalid data 1 7.7 

# I.' 0 .S1 

# '18 1.7 16.8 2.5 1 ,01 128 3/ 17IC8 16:45 3'7 28 .3 1 32
-0.18 3.4 19.2 12 0.89 

# I" 28 1 8.9 1. 5 0.84 "0 IflvaliddaJ a 17.7 

# ,.s 0 .82 

# '18 ' .7 16.8 2.5 1 .02 127 3.'17iC817 :00 3&3 28 .30 29 · 0. 18 4.0 19.2 1.2 0 .85 " 0 3.1 1 8.9 1 .5 084 109 I nva td nata 17 ,7 

# ,

# . 0 .82 117 1.' 16.8 2.5 1.02 126 311

7IC8 17:, 5 

# 3S' 2630 26 -0. 18 4.2 19.2 1.2 0,87 109 3.4 1 8.9 1. 5 0.84 10' I rwa' id d.J.ta 17.7 

# I .' 0 .62 

# ' 18 , .o t6.8 2.5 

## t .oo 125 3/ 17iC8 '7:30 300 28 .30 27 -0. 19 5 .2 19.2 1.2 0.86 109 4 .0 1 8.9 '5 0.84 las I nvalid data 17,7 

# I .' 0 .82 " 5 2.' 16.8 2.5 1.00 

### 'N 3/ 17iCS 17:45 39 1 28 .30 26 · 0.19 5 .1 19.2 1.2 0.87 109 4.' l S.9 1 ,5 0 .84 108 lnva.lo'da ta. 17,7 

## ,.s 0 .82 11 5 2' 16.8 2.5 1. 0 1 12 4 3/ 17"08 18:00 3 0;2 26 .30 26 · 0. 1 9 5 .5 192 1.2 0.89 

### '09 4 .4 1 8.9 1.5 0 .83 108 Irwaic1 da la 17.7 

# I. , 0 .82 

## u e 2 .' 16.8 2.5 0.99 125 3/ 17

/0818: 15 383 26
.30 26 -0. 19 5. ' '9.2 '2 0.87 

## ros 4 .5 1 8.9 

# I. ' 0. 82 108 lnvaid data 17. 7 

# ,

# . 0 .8\ 1\5 2 .2 16.8 2.5 0.99 125 3 .'17

106 18:30 394 26
.29 26 -0.19 4.7 '9.2 '.2 0.87 108 37 18 .9 1. 6 0. 84 108 lnv»d da ta '7.7 

# I.' 0 .8\ "5 2.0 18.8 2.5 0. 99 1 25 3.r17

/ CS 18 :45 395 26
." 26 -0. 19 4.' 

### '9.2 ' .2 0.85 

# lea 3 .9 1 8
. 9 1. 6 0.84 '08 InYaid data. 17.7 

# . .• 0 .83 115 20 16,8 2.5 1.00 1 25 3/17/09 19 :0) 396 29
.26 29 -0.19 4 .4 19.2 ' .2 0 .89 107 3 .8 1 8 9 

# I.' 0.85 

## ioa IrwMd d al a 17.7 

# ,

# . 084 "5 2' 16.8 2.5 1 ,02 124 3 '/17,OS 1 9 : 15 397 

### 2827 2S

-0. 1 9 5.4 19.2 1.2 0. 89 

# .ea '
.4 18 .9 1.5 0.85 

# , ea \ovaIId data 1 7.7 

# ,

# . 0 83 

# us 2.3 

### . 6.8 2 .5 1 ,02 124 3,/17

/05 19 :30 '96 29.27 

### 2S -0
. 19 5 .6 19 .2 ' .2 0
.B7 

## r es 4 .' 18 .9 

### i
. s 0.83 

## ica I n vaWdata 17.7 

# I .' 0 83 115 2.3 

### . 6.8 2 .5 0.93 124 3.'17i C9 19 :45 

# 39' 28
.27 25 5
. ' 192 1.2 0
.80 

# ic s 4 .' 18 .9 

# I. , 0 .83 

# , ea**~dat** 17.7 

# ,

# . 0
.91 11 5 2.2 16 .8 2 .5 0.97 125 31 17 .08 20 :00 400 28.27 25 -0
. 19 5.0 19 .2 

### t.2 0 .87 

## r e s 4
. 1 18.9 

# I.' 0 .32 

### rca Invaid dal
. 17.7 

### t.. 0 .81 11 6 2.e 16.8 2 .5 0.9i$ 125 3' 17

;03 Z115 401 

### 28 26 25 -0
. 1 9 3.5 19.2 1.2 0 .8 9 

## r ca 3
.0 18 .9 

# . .• 0. 85 

### rca Invaid dal
. 

### 17
. 5 1
.• 0 .8 1 115 

# I. , 16.8 2 .5 0." 125 3117

, 00 20 : 30 402 28 .26 25 -e . 1 9 4
. '- 19.2 

### ' .2 0 .00 

# lea 3 .7 

### 'B' 

## ,.s 0. 83 ' 07 Ir'lvdd d ata 17
. 9 

### 20 0 82 115 

# I. ' 16 .8 2 .5 0.99 124 

### 311710820: 45 40 3 28 .25 26 -:J
. 19 5 .5 19.2 ' .2 0
.68 I e, 4
.3 18.9 

# ,

# . 0. 84 103 InvaItd d a:a ' 7.7 

# I .' 0
. 8 1 115 

# ,,4 16.8 2 .5 0 .96 124 404 2625 26 -0. 1 9 5
. 1 19.2 ' .2 0. 69 

# ics 4
.0 

### '8 .9 

# I.' 0
. 84 

# lea InvaIid dala 17.7 

# ,

# . 0 .81 115 

### 21 '6.8 2 .5 IN 405 28 .25 2.
- :J. 19 5.2 '9.2 ' .2 0
.68 110 40 'S ,9 t
. • 0. 82 10> l nvalld dala 17.7 

# I.' 0
. 81 11. 21 

### .B8 Z5 ' 25 4C<l 2825 26 -0. 1 9 4 .8 19 .2 ' .2 e . 85 111 3' ' 8.9 

# ,

# . o.as I e , Invaid dalil 

### 17.7 

# I .' 0 .8 1 

# " ' 21 1 7
.2 Z5 ' 25 407 

### 2826 2. -0
. 19 4.3 '9.2 ' .2 0. 8& 110 3
. ':- 18.9 

# I .' e .83 I e ,**i! 1a**  

### 17.7 

### t.' 0 .60 110 2 0 17 .1 2 .5 ' 25 

# -cs 2625 

### 26 -0.19 4.' 19.2 ' .2 0 68 Ie> 3
.3 1 8.9 

## , .e 0 .84 

### rca 

# """"" - ' 7.7 

## ,.s 0 .82 116 2 0 17
. 1 Z5 1 25 40 ' 26 .25 2' · 0.19 5.2 192 

### t.2 0 .68 "0 4 .' 18, 9 

## ,.e 0 .62 

### rca nvaJ ::idala ' 7.7 

### t.' 082 

# "' Z2 17
. 1 Z5 125 ':' 10 

### 2825 27 -0 .19 5 .' '9.2 12 0 .68 "0 4. 0 18.9 

# I.' 0.83 

### rca I nva6d data '7. 7 

# I .' 0 .83 11. Z I 1 7.0 25 1 26 4" 2624 

### 27 -0.20 5 .3 19.2 '.2 0.89 

### '09 42 t8.9 

## t.e 0.82 

## ics I nvilf d data 17.7 

### t. . 0 62 116 22 16.9 25 1 26 412 2924 27 -0.'"' 4 .2 19.2 1.2 0.90 

# ,ea 35 18.9 

# ,

# . 0.86 

## ics Invaid_ 

### 17.7 

# I
.' 0 83 

## ne 2.1 16.9 25 1 25 413 28 .ZJ 27 -0.2J 5.5 19.2 ' .2 0.89 ,e, 4.4 18.9 

## ,.e 0. 85 

### res nvaid dat a 17, 7 

# ,s 0 .83 1 1 6 24 16.8 25 124 4 14 28 .22 27 -0. 19 6.0 19.2 1.2 0.68 " 0 4 .' 18.9 

# ,

# . 0 .84 "0 1m. '3tId daLa 17.7 

# I.' 062 

# ". 2 .5 16.8 2.5 125 ':"5 29 .22 27
-0. 19 52 19.2 1.2 0.68 "0 4
.3 18.9 

# ,.e 0.84 110 InvaI:d daLa 17,7 

# I,' 0 .62 "7 22 1 6.8 

### 25 126 4,. 29.22 27 -0 .19 5.3 19.2 '.2 0.89 

# ic s 4.3 18.9 

# ,

# .. 0.84 

### rca Invakl d31a 17
. 7 

# I
.' 0 .83 

## ue 2.3 1 6.8 2 .5 125 4 '7 2621 27 -0.19 5.' 19.2 1.2 0.68 

# ,,, 4 .4 18.9 '.B 0.84 

## ics WlvlDd d all1 17.7 

# ,.s 0 .83 116 2. 4 1S.8 25 125 4 16 28 .2 1 27 -0.19 4.7 19.2 '.2 0 .00 

# ic s 3. ' IS.9 '.B 0.84 

## tea kMl!id d ala 17.7 

# I.' 0.83 '16 2.2 16.7 2.6**1~6** 4'
. 28.20 27 -0.19 5' 19.2 1.2 0.90 

# ic s 4
. 2 18 .9 I.B 0.66 

## ics In vafddata 1 7.7 

# I.' 0.63 11 6 2,4 16.7 2 .6 125 4 20 2S.20 

### 27 -0 .19 '.0 19.2 •.2 0.89 "0 4.a IS.9 '.B 0.84 "0 Iovalld da l3. 17,7 

# ,

# . 0.83 ' 16 2.' 16.7 2 .5 ' 25 42 1 2$ .19 27 -0. 19 4.7 19.2 ' .2 0 .90 

### res 3.s 18.9 I.B 0.84 

### rca 

# """"' daI
. 17 ,7 

# I.' 0.63 

## u e 23 16.7 2.5 125 422 28 .' S 27
-0.19 4.8 19.2 1.2 0.90 " 0 3. 9 18.9 1.6 0.84 "0 ln ve re dat a 17,7 

# I.' 0.63 

## us 22 16.7 25 ' 25 

### 423**~a .18**  27 -0,' 9 4 .6 19.2 ' .2 0.S9 

## ics 3 .a 18.9 

# ,.s 0.84 

### res In"*' 

## cara 

## trr 

# I.' 0.84 

## us 2.2 16.7 2.' 125 .:.2

4 28.17 27 -0.19 4 .7 19.2 1.2 0.89 

# 'C. as ,6.9 

# , 

# .. 0.84 109 InvaIid d a13 1 7,7 

# I.' 0.84 

## ue 22 16.7 2.' 1 25 ..25 28
. 16 27 -0.19 4 .9 '9.2 ' .2 0.89 109 4 .0 1S .9 1.B 0 ,84 109 I nva:Kldata. 1 7.7 

# I .' 0.83 

## u s 2.3 16.7 26 125 429 28 .15 27 -0.\ 9 4 .7 19 .2 '.2 0.00 "0 

# a.s 18.9 1.B 0 .84 l OS I nvalid d a ta 1 7.7 

# I.' 0.83 " 6 2 .2 16 ,7 26 12 5 427**~8 15**  27 -0.'9 4 .3 19 .2 ' .2 0. 89 110 

# s.s 1 S.9 

# ..• 0. 84 109**daf 3.**  ' 7.7 

# I.' 0.82 117 

### 21 16 .7 26 12' 428 28 .\5 27 -0.\9 3.6 19.2 ' .2 0 .91 109 3 .' 1S .9 ' .B 0. 86 109 Inva::id d ata 17 ,7 

# " 0 .84 

## u s 2' 16.7 2.• 125 

# ..a 28 .15 27 -0.19 4 .4 192 ' .2**.~** " 0 3. 6 18.9 ' .B 0.66 109 lr:v a 'id dab 17. 7 

# I .' 0 .84 11 6 22 16.7 2.6 125 430 2'8.14 27 -0
. 19 4 .' 

### '9.2 ' .2 0 .91 110 3 .7 18. 9 ' .B 0.8 5 ' 03 [ nvaici da!a 17
. 7 

# I .' 0 .83 116 2. 3 16,6 2.6 1, 5 

### 43' 28
. 14 27 -0. 19 4 .7 19 .2 ' .2 0. 9':1 110 3 .' 18 .9 t
.• 0.85 " 0 Invaid d atil 1 7.7 

# I .' 0 .83 

## ne 2,4 \ 6.2 2_0 124 432 28
. 14 27 C
. 19 4
.7 19 .2 ' .2 0 "" 

# " '**~O** 

### , 6.9 

# ,

# . 0.a5 110 lnvald da ta '7.7 

# I
.' 0. 84 "6 2.5 16.6 2.' ' 24 433 2a .13 Z1
-0. 1 9 4
. 9 19 .2 '.2**O.** .11 4 .0 

# ,8.. 

# ,

# . 0 ,86 110 Invaid d
.... 17. 7 

# I .' 0
.05 

## rts 2 .5 16.7 2.' IN 

### 43' 28.13 27
- :J. 1 9 52 '9.2 '. 2 0. S9 111 4 2 

# , 8.' ' .B 0 83 110 

# , '''''''_ '7.7 

# I .' 0.83 117 2.5 1 6 .7 26 114 435 26
. 12 27 -:J. 1 9 4
.a 19.2 ' .2 0. 68 3
. ' 

### lB ' 

# 1.. 0
. 84 110 InvaJ,.:Jd ata. 17.7 

# I .' 0 .83 117 24 18
.8 2.6 125 436 20 .12 27 -0
. 1 9 4
. ' ' 9.2 '
.2 0. 68 112 3
. ' 18.9 t
. • 0. 84 110 Inv'Ud d ll la 17.7 

# I .' 084 117 Z3 16 .9 2 .5 125 43 7 2012 27 -C
. 1 9 5.0 '9.2 1 2 0. S 9 112 4
.0 ' S.9 t
. • 0. 84 110 Irw»d dat a 1 7.7 

# I .' 0. 83 :1 7 23 17 .0 2 .5 125 

### 438 28
. 11 27 -0
. 1 9 5
. 1 '9.2 1. 2 0. 89 112 40 18.9 I. B 0. 84 110 kwal d data 17.7 

# I
.' 0 84 117 23 17
.0 25 '25 439 28 .11 26 -0
. 19 5.3 '9. 2 ' .2 0. 90 11 1 4 .1 lB.9 t
.• C
. 64 110 Inv<dtd data 1 7.7 

# ,.s 0 .84 11 7 25 16 .9 Z5 ' 25 

# """ 28.12 2.
-0
. 1 9 5.6 '9.2 1.2 0
.S9 11
. 4' ' S.9 1.B 0 .65 110 Invaid da lll 17 .7 

# I
.' 0 .84 117 27 17 .0 Z5 124 44' 28 .1 1 27 -0.19 5 .5 '9.2 ' 2 0
.68 112 4 .5 1S.9 

## t.e o.es 110 malrd dalll 17 .7 

# I
.' 084 117 28 17 .0 25 1 24 442 28 .1 ' 2. -C. 19 5. 5 19.2 ' 2 0
. 89 112 4 ,4 1B. 9 ' .B 0 64 110 

# """"' - 17.7 

# I .' 0 84 117 27 1 6 . 9 25 12_ 443 2811 26 -0. 19 5.7 19.2 ' .2 0 .90 "2 4' IB .9 

# ,.e 0.86 "0 InvMd da la 17
. 7 I. ' 0. 83 117 2S 1 6 .9 2 .5 125 444 28 .1 ' 2. -0. 19 6 .' 19.2 ' .2 0 .S9 "2 4.9 18.9 ' .B 0.84 "0 tnvalld d.1ln '7. 7 

# ,

# . 0
. 83 117 3. 0 1 6.9 2 .5 1 25 445 28 .10 27 -0. 19 5 .' 19.2 ' .2 0 .89 112 4.8 18.9 

# ,.e o.ss "0 nvakf da la ' 7.7 

# I. ' 0 ,8 3 117 3 .0 16.9 2 .5 1 25 446 28 .10 27 -o. 2,J 

# •. , 19.2 1.2 0.89 "3 5
. 1 18.9 1.B 0 84 II' rnalicf dala 17.7 

# I .' 08 5 117 3.2 16 .9 2.4 125 447 28 .09 27 -0 20 62 19.2 '.2 0.68 " 3 5 .1 IB. 9 I.B 0 .85 "0 Invaid

_ 17. 7 

# I
.' 0 .64 117 3 .2 16 .9 2. 4 124 

### 44B 28 .09 26 -0 .19 6.2 19.2 '.2 0.87 "2 5
. ' 18.9 

## ,.e 0.85 "0 

### Iovalid data ' 7.7 

# I.' 084 117 3 .2 16 .9 2.5 1 24 44
. 28.09 2. · 0.19 6.3 19.2 1.2 0.68 II ' 5.3 18.9 '.B 0.84 "0 In vakl data 17 .7 

# I.' 0 .84 '16 3.5 17 .2 2.5 12 4 

# aso 28.08 26 -0.19 2.7 7. ' 1
.3 0.68 112 5.6 18.9 '.B 0.84 110 

# """"' - ' 7.7 

# I.' 0.83 117 3.8 '6.8 2 .5 124 45' 28.08 27 -0.19 7 ,4 17, 8 '
.2 0.66 " 2 4. ' 18.9 I.B 0.84 "0 Irwahd da ta 17 ,7 

# I.' 0.83 11 6 3 .6 16.8 2 .5 '24 AMlyz w 

### CMbfa lion 452 28.08 27 -C.19 7
. ' 1 9
. 1 1 .2 0.87 " 2 5 .7 18.9 '.B 0.63 "0 nvaid da t a 1 7.7 

# I.' 0.63 1 16 3.' '6.8 2 .5 124 Sy slem B6as D rif t ChEc k 2$.07 27
-0.19 B. ' 11
.2 0 .' 0.69 " 2 5 .5 18.9 1.B 0.84 "0 In Vlltid

da t

a 17.7 

# I.' 0.63 116 '
.4 18,6 2 .5 1 24 454 28 .08 27 -0. 19 

## s.s 1. 3 0
. ' 0.68 " 3 56 18 .9 1.B 0.83 "0 In vattd da: a 17 ,7 

# I. ' 0.83 

## us 3.8 16.8 2.5 12 4 455 28.08 27 -0. 19 3 .5 1 5
. 7 2 .0 0.87 " 3 5
.5 18.9 '.B 0.83 110 JnvakI data ' 7.7 

# I.' 0.8-3 117 3.6 16.8 2.5 125 3!1 8iOe 1 0:00 

### .;s6 28 .09 27 -0. 19 4
.0 1 9
.9 0 .' 0.68 "3 4
. s 18.9 '.B 0.83 "0 IfIova£cI da:.a 17 .7 

# ,.s 063 116 3.2 16.S 2.5 0 .97 124 31 1ao'0610 : 15 457 28 .09 2S -0. 19 7 .' 19.5 1.2 

### 0.B6 " 3 5
. 5 

# 1 8.. I.B 0.83 "0 lnvaAd da la 1 7.7 

# . .• 082 "7 36 16.8 2 .5 1. 01 1 24 31113.'06 1 0:30 

### 45S 

### 28 OS 28 -0. 19 7 .0 1 9.5 j.2 0 .86 112 5 .3 18.9 I.B 0.83 "0 Invaid da '" 1 7.7 

# I.' 0 ,82 117 3,5 16.8 2.5 1. 03 124 31 18108 1 0:45 45' 28
.08 28 -0.18 •. 7 , . 5 12 0 .87 "3 5 .0 18.9 I.B 0 .63 110 lnwlid da ta 

### 17 .7 

# ,

# . 0.63 " 7 3,4 17.9 2.' " 04 124 3 1 1 i!.

'061l :C ·,) 460 2806 29 -0. 18 6.7 1 9.5 1.2 O .BS "3 5 .1 18 .9 ' .B 0 84 " 0 Inv;:Wd data 17. 7 

# I .' 0 .83 117 33 17.9 2.4 ' 06 1 2 4 3I 1 3J(l6 1l:l5 46' 2806 30 -0 .17 •. 8 19.4 1.2 0 .87 113 5 .2 '8 .9 I. B 0. 64 110 I nvaJodd:1la 17.7. 

# I., 0 .82 "7 3 .5 17.9 2.' 1 ,CS 1 2
.. TOA5**TI~.~ESTA~.~P** TS 3.'1 7ies 16.00 3117/08 16:15 3.'17/08**~6:30** 311710816 :45 3.'17/C917:00 3117iC817:15 3117/08 17:30 3117i08 17:45 1il7/0818:00 3117/0818:15 1 ' 17106 18:30 1'17/(! 918:45 l ' 171

0919 :Oo) 1 ' \7, 0919:15 l ( 17fOS 19 : 30 l ' \7i 09 19 :45 3117
. 0820: 00 l ' I7 1

03 20: 15

3111!/06 10 : 15 31181 06 10:30 31,8108 10:45 3 ' I B/06 11:C") 3I18IOB 11:15 

# I STACK A- 

### inputs STACK 

## B- inputs J'\O
..**CE.'~S** CFll000 4789 ::;,000.Std.es T atri lS RECORD**(1I"?r~s_A\rTmp_F**_A>3tatcP_A\'{302_AYG{1**~Avg (I)::02_Avg(** **1 ~rRow** **V(T mp_F** **_AY~2-Mg{,** 02.-Avg(:2):xY.i!_AYO(2.ifFloY.-2_Av.TffiP_F_A

RN**~'"IHg** Deg F LIOH20 ppmDry Pfe niOty PcntOry inH20 Deg F ppmDry PrentOry PenlDry nH20 Ofog F 384 385 

### 386 397 

# 38' 3., 39 1 392 393 394 395 396 397 396 

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# "" 402 403 4C' 

### 405 4C<i ",7 

# "'" 40 ' ':' 10 

# '" "2 

### "3 

# 41. '19 

### '20 421 ..", 

### -123 

### '2'**~25** 426 '27 ",. 

### 431 432 433 

# '"' oilS 436 

### 0137 438 oil' 

### «IJ

447



# ..... 449 

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# , 

# ... 455 456 457 

### 458 459 

# ""0 ",,1

# ~**~ ~**  

# - - 

# - - 

# - - 

# - - 

# - - 2B
. 31 28 -0.18 5.2 19.2 1.2 0.88 109 4.1 la.9 1.6 0.83 108 28
.31 30 -0.18 4.7 19.2 1.2 0.88 '" 3
.6 IS.9 1.6 0.83 110 28
. :30 33 -0.18 3.8 19.2 1.2 O.BS III 3
.0 18.9 1.6 0.84 ", 2B
.31 32 -0.16 3.4 19.2 1.2 0.89 

# 1" 2
. 8 18.9 1.5 0.84 110 2S
.30 29 ·0.18 4.0 19.2 1.2 O.SS 110 3
. 1 18.9 1.5 0.84 109 28
.30 28 ·0.18 4.2 19.2 1.2 0,87 109 3
.4 la.9 \.5 0.84 108 28
. 30 27 -0.19 5.2 19.2 1.2 0.86 109 4
.0 18.9 1,5 0.84 108 28
.30 26 ·0.19 5.1 19.2 1
.2 0.87 109 4
. 1 lS.9 1,5 0.84 loa 

### 28
.30 26 · 0.19 5.5 19.2 1.2 0.89 109 4.4 18.9 1.5 0.83 108 28
. 30 26 -0.19 5.6 19.2 1.2 0.87 109 4
.5 18.9 1.6 0.82 108 28
.29 

### 26 -0.\9 4.7 19.2 1.2 0.87 

### lOS 3
.7 la .9 \.6 0.84 108 28 .29 26 -0.19 4.8 19.2 1
. 2 0.88 lea 3 .9 IS .9 \.6 0.84 108 

### 28.28 26 -0.19 4.4 19.2 1.2 0.89 107 

### 3
.8 18
. 9 

### \.6 0.65 lea 29
. 27 25 ·0.19 5.4 19.2 1.2 0.89 108 4.4 18
. 9 1.5 0.85 lea 29
.27 25 .0.19 5.6 19.2 1.2 0 .87 lC9 4
.6 18
. 9 1 .6 0.83 lea 28.27 25 ·0
. 19 5 .9 

### '9.2 '.2 0. 80 lCg 4
.8 18.9 1.6 0.8.3 lea 28
.27 25 -0. 19 5.0 19
. 2 

### '.2 0.87 IC9 4
. 1 18
.9 1.6 0 .82 lC8 28
.26 25 -0. 19 3
. 5 19.2 1.2 0.89 l ea 3 .0 '8.9 '.e 0. 85 IC8 28
.26 25 -C. 19 4
. .. 19.2 1.2 0.90 lea 3
. 7 18.9 1.8 0. 8.3 107 28
.2.5 26 -0.19 5
. 5 19.2 1.2 0.88**C~** 4
.3 18.9 1
. 6 O. a.a 108 28 25 Z6 · 0. 19 5
. I 19.2 1.2 0.69 l C9 4 .0 18.9 1.6 O.a.; lea 28
.25 26 · 0. 19 5.2 19.2 1.2 0. 88 1 10 4
.0 18.9 1.8 0. 82**~** 28
.25 26

-0. 19 4.8 19.2 1.2 C.88 III 3
. 8 18.9 1.6 0. 85 l C3 28
.26 26 -0.19 4.3 19.2 1.2 0.66 110**~** 18.9 1.6 C.8.3 l C3 28
.25 

### 26 ·0.19 4.1 19.2 1.2 

### O
.OS**lC~** 3 .3 1B.9 

### '.8 0.84**C~** 28
.25 

### 2u ·0.19 5.2 19.2 

### 1.2 O.as 110 4
. 1 lB.9 

### '
. 8 0.62**IC~** 28
.25 27 -0
. 19 5.1 19.2 1.2 0.88 1'0 4 .0 1B.9 1.8 0.83 lC3 28
. 24 V -0.20 5.3 19.2 1.2 0.69 109 4
.2 18
. 9 1.8 0.82 lC3 29
.24 27 ..<J.20 4.2 19.2 1.2 0.90 lea 3
. 5 18.9 

### t.6 0.80 lC3 28
. 23 Zl ·0.20 5.5 19.2 1.2 0.89**lC~** 4.4 1B.9 1.6 0.85 IC9 28
.22 27 -0.19 6.0 19.2 1.2 

### O.as 110 4
. 8 18.9 1.6 0.84 "0 28
.22 27 ·0.19 5.2 19.2 1
. 2 0.88 110 4
.3 IB.9 1.6 0.84 110 28
.22 27 -0.19 5.3 19.2 1.2 0.89 le 3 4
.3 18.9 1.6 O.a.a**lC~** 28
.21 27 -0.19 5.6 19.2 1.2 0.88 10 3 4
.4 18.9 1.6 O.a.a IC9 28
.21 27 ·0.19 4.7 19.2 1.2 0
. 90 le 3 3.8 18.9 1.6 0.84**lC~** 23
. 20 27 ·0.19 5.1 19.2 1.2 0.90 le 3 4.2 18.9 1.6 0.86 IC9 26
. 20 

### 27 ·0. 

### I 9 6.0 19.2 

### 7.2 0.89 110 4.8 18.9 1.6 0.84 110 2$
. 19 27 -0.19 4.7 19.2 1.2 0.!Xl IC9 3.9 78.9 1.8 0.B4**IC~** 

## :as .'S 27 ·0.19 4.8 19.2 1.2 0.!Xl 110 3.9 18.9 

## 1.6 0.84 110**~a 1B**  Z1 -0,,9 4.6 19.2 1.2 0.89 '09 3.B 18.9 1.6 0.84 lC9 28
. 17 27 -0.19 4.7 19.2 1.2 0.89 lC9 3.8 18.9 1.6 0.84 109 28.16 27 -0.19 4.9 19.2 1.2 0.69 109 4.0 1B.9 1.8 0,84 109 28.15 27 -0.\9 4.7 19.2 1.2 0.90 110 3
.6 18.9 1.6 0.84 109**~a .'** **5** 27 -0.19**~.3** 19.2 1.2 0.8 9 110 3
.6 '8.9 1.6 0.84 109 28 .\ 5 27 -0.19 3.6 19.2 1.2 0.91 109 3.1 lB.9 1.6 0.86 109 28 .15 27 ·0.19 4.4 19.2 1.2 0.50 11 0 3 .6 18.9 1.8 0.86 \ 09 28
. 14 27 ·0.19 4 .6 19.2 1.2 0
.91 110 3.7 18.9 1.8 0.85**10~** 28
. 14 27 -0. 19 4.7 19.2 1.2 0
.9:J 

## no 3.9 

### 18.9 1.6 0.85 \\0 28
. 14 27 · C. 19 4
. 7 19
. 2 1
. 2 0
.9(.) 111 4.0 18.9 ,.6 0.85 \\0 2a
. 13 Zl · 0. 19 4 .9 19.2 1.2**O. ~l**  I I I 4
.0 18.9 1.6 0
.80 110 

### :2& 13 27

-0. 19 5

_ 2 19
.2 1.2 0. 69 I I I 4
.2 18.9 1.8 0
.8.3 110 26.1 2 27 -0. 1 9 4
.0 79
.2 1.2 0. 88 1 12 3 .9 18.9 

### '.8 O. a.a 110 20.1 2 27 -0. 19 4
. 9 19.2 1.2 

### O. as 1 12 3 .9 18.9 

### '.6 0. 84 110 28
. 12 

### 2:l ·C
. 19 5.0 19.2 1.2 0.69 1 12 4, 0 18.9 1
. 6 O. a.a 1 10 28
. 1l 27 -0. 19 5
. 1 19.2 1.2 0. 89 112 4 .0 18.9 1.6 O. a.a 1 10 28.11 26 -0.19 5.3 19.2 7.2 0.90 1 11**.1** 18.9 1.6 C.04 110 28.12 26 -0 .19 5.6 19.2 1.2 0 .69 I I I 4
. 6 18.9 1.6 0 .85 110 28
. 11 Z7 -0.19 5.5 19.2 1.2 

### O.OS 112 4.5 18.9 1.6 0.85 110 28
. \\ 26 -C.I9 5.5 19.2 1.2 0.89 \\2 4.4 18.9 1.6 0.64 110 28
. 11 26 -0.19 5.7 19.2 1.2 0.90 112 46 1B.9 1.8 0.66 1 10 28
. 11 26 -0.19 6.1 19.2 1.2 0.S9 1 12 4.9 18.9 1.6 O.a.a 110 2a
. l0 27 -0.19 5.9 19.2 1.2 0.89 112 4
. 8 18.9 1.8 0.65 \\0 2B
. l0 27 -O.2.:J 6. I 19.2 1.2 0.89 113 5
. 1 18.9 1.6 0.84 I I I 28
.09 27 -020 6.2 19.2 1.2 0.88 113 5
. 1 18.9 1.8 0.85 no 2B
.09 26 -0.19 6.2 19.2 1.2 0.87 112 5
. 1 18.9 1.6 0.85 no 2B.09 26 ·0.19 6.3 19.2 1.2 0.88 11 I 5
.3 18.9 1.6 0.84 \\0 28
.08 26 ·0.19 2.7 7. 1 1 .3 0.88 "2 5
.6 18,9 1.8 0.84 110 26,06 27 -0.19 7.4 17, 6 1
.2 0.88 112 4.6 18.9 1.8 0.84 110 

### la
.OS Zl -C.19 7
. 1 1 9. 1 1.2 0.87 112 5
.7 18.9 

### 1.6 0.83 110 28
.07 27 ·0.19 6 . 8 1 1 .2 0.6 0.059 112 5
. 5 18.9 1.6 O.a.a 110 28
.08 27 ·0.19 6 . 9 1. 3 0 .1 0.88 113 5
.6 18.9 1.6 0.33 110 23.0S 27 -0.19 3.5 1 5.7 2.0 0.87 113 5
.5 

### 18.9 1.6 0.83 110 28
.09 27 ·0.19 4
.0 1 9.9 0.8 0.88 113 4
. 9 18.9 1.8 0.83 110 28
.C9 28 ·0.19 7.1 19.5 1.2 0.66 113 5
. 5 18.9 1.6 0.33 110 

### 28
.09 28 -0.19 7.0 19.5 j.2 0.66 112 5
.3 

### 18.9 1.8 0.83 110 28 .03 28 ·0.16 6.7 1 95 1
.2 0.81 113 5
.0 16.9 1.6 0.8.3 110 28
.06 29 -0.18 6.7 19.5 1.2 0.80 113 5
. 1 18.9 1.6 0.84 110 28
.06 30 -0.17 6.8 19.4 1 .2 0.87 113 5
.2 18.9 1.6 0.64 110 In valid oaT.l. I nva'id d.J.ta Invalid d.lta Inva.'id data Irwald dal.l. I nvaid data 

### I nvaid dal.l. 

### Invalid data. lrwaid data. !ovaftd data In .-aid da13. tnvaiddat a 

### 1fflaiddal
. 

# """"" 

# .... 1nVoId d "" InvaIid da:a InvaIid dala I nvalid dala InvaIid dala Invaid data 

# """"' data 

# """"data Invalid data. Invilfld dam 

# _data Inwid daTa 1m.'2id daLa IrwaId daLa InvaId dala vwaid datn VlvaMd dilla In valid data lova6id da!a 

### """"' data Inval.

' ddala 

### In

_ data InvaIid dal.3. Invalid data Inv<n:l d al a 

# """"' - In
...;Dd data 

# Inv"" """ I nvaid dolIa Irwaid d.:1la 

### Invaid dala Invaid dala 

# , 

# ......

# _ InvaEd d ata IrMdid d ata IrwaIid d ata**kwaI ~_**  Iov;1Iid d ala Invaid d ata InvaId data. 

# """' - InvaIid da!a 

# """" ""'a Invalid dala V1vaIid d3.la 

# """"- .,vaIid data In vaid data """d dala lnvatiddata Invalid dafa In vM:<:l dal a In valid data 

### InvatId data 

# I<Moid d,,,. Invaid data 

### Wwaid data 

### Inwld 

### data ln v;:lld dala 

### I nvaJid <bla 

### STACK C· 

### inputs

17.7 1.9 17.7 1.9 17.7 1.9 17.7 1.9 17.7 1.9 17.7 1.9 17.7 1.9 17.7 1.9 17.7 1.9 17.7 

### 1
. 9 17.7 1.9 17.7 1
. 9 17.7 

## ,.9 17.7 1
.9 17.7 1
. 9 

### 17.7 1
. 9 17.7 1.9 

### 17.5 I
.g 17
. 9 2.0 

### 17.7 1
. 9 17.7 1.9 17.7 

### r.9 17.7 

### f.9 17.7 

### f.9 17.7 1
. 9 17.7 

## '
.9 17.7 1
. 9 ".7 1.9 17.7 1
. 9 17.7 1.9 17.7 1
. 9 17.7 1.9 

### 17.7 I.S 17.7 1.9 17.7 1.9 17.7 1.9 17.7 1
. 9 

### 17.7 1.9 

### 17.7 1
. 9 

### rl.7 1
. 9 17.7 1.9 17.7 1.9 17.7 1.9 17.7 1
. 9 17.7 

### 1
.9 17.7 1
. 9 17.7 

## '.9 17.7 1.9 17.7 

### f.9 17.7 1.9 17.7 1.9 17.7 1, 9 17.7 1
. 9 17.7 1.9 17.7 1.9 

### 17.7 1
. 9 17.7 1
. 9 

### 17.7 1
. 9 17.7 1.9 17.7 1
. 9 17.7 1.9 

### 17.7 1.9 17.7 1
. 9 17.7 1
. 9 17.7 1.9 

### 17.7 1.9 17.7 1.9 

### 17.7 1.9 17.7 1,9 17.7 1.9 

### 17.7 1.9 17.7 1.9 17.7 1.9 17.7 1.9 17.7 1.9 

### 17.7 '.9 17.7 1.9 17.7 ' :.. 9 0
.81 0
. 80 0
.61 0
. 82 0
. 82 0
. 82 0
. 82 0
. 82 0
. 82 0
. 81 O
.Bl 0.83 0
.94 0
. 83 0
. 83 0.S1 0.61 0.81 0
. 82 0.8 1 0
. 81 0.8 1 0
. 81 0.80 0
. 82 0
. 82 0
. 83 0
. 82 0
. 83 0
. 83 0
. 82 0
. 82 0.83 0
. 83 0.83 0.83 0.83 0.83 0." 0.84 

### O.g.; 0.83 0.83 0.82 0.84 0.84 0.83 0.83 0.94 0.05 0.83 0.83 0
.94 0. 83 0
. 94 0
. 84 0
.94 0
.94 0
.94 0 .83 0.83 0
. 83 0
. 85 0.84 094 0
. 84 0.83 0.83 

### 0." 0.83 0.83 0.83 0
. 83 0,62 0,62 0.83 0.83 0.82 

### STACK [). 

### inputs Avg(1 D2_Avg{4}:;02-Avg(4.i rflow4_AdtTmp_F _Avg(4 ) PPffiDry PfcntOry PenlOI)' inH20**~** F

# ""''''**2~ '-** **:~ ~1** **~~ ~;~**  117 11. 118 117 116 115 115 11. 115 115 115 115 116 115 115 116 115 115 115 115 

### Tlo 11. 110 116 "6 

# ". lIS 116 

# , ,6 116 117 116 116 

# ". lIS 11. 116 116 116 116 116 11. 117 116 116 116 11. 11. 11. 117 117 117 :1 7 117 117 117 117 117 117 117 117 117 117 117 11. 117 lIS 11. 

# 11. 116 117 11. 117 117 117 

# ," 117 \.8 16.8 2.5 1.01 126 \.7 16.8 2.5 1,0\ 128 1.7 16.8 2.5 \.02**~27** 1.8 16.8 2.5 1.02**~26** 1.9 16.8 

### 2.5 1.00 125 2.1 16.B 

### 2.5 1.00 124 2.1 16.8 

### 2.5 1.01 124 2.1 16.B 2.5 0.9g 125 2.2 16.8 

### 2.5 0.99 125 2.0 2.0 21 2.3**~3** 2.2 2.0 1.3 1.' 

### t .•**1 ~1** **~1** 2 0**o ~2**  2. 1**~2** 2.1**~.** 2.5 22**~3** 2.' 2.2 2.4 2 .• 2.3 22 2.2 

### 22 2.3 2.2 2.1 21 22**~3 ~,**  2.5 2
. 5 2.5**~4 ~J** **~J ~3**  2
.5 

### V**~.** V 

# 2. 3.0 3 .0 3.2 3.2 3.2 3.5 3.8 3 .• 3 .• 

### 6 .' 3 .• 3.6 3.2 36 3,5 3.4 

### 33 3.5 16.B 16.B 16.8 

# ,6." ,6." 16.8 16.B 16.8 '6.8 16.8 16
. 8
17
. 1 17
. 1 17
. 1 17.0 16.9 16.9 16.8 16.8 16.8 105.8 16.8 16.7 16.7 16.7 16.7 16.7 16.7 16.7 16.7 16,7 16.7 16.7 16.7 16
. 6 \6. 2 16.6 16.7 16.7 IS
.8 16.9 17
.0 17
.0 16
. 9 17
.0 1 7
.0 16
. 9 16.9 16.9 16.9 16.9 16.9 105.9 17

_

2 f6.8 16.8 16.8 16,8 16.8 16.8 16.8 16.B 16.8 

### 17.9 17.9 17.9 

### 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2
.5 2.5
2
.5 2.5 2.5**~5 ~5** **~5** 2.5 2.5 2.5 2.5 25 2.6 2.6 2.5 2.5 2.5 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2
. 6**~6** 2.6**~6 ~6**  2
.5 2.5 2
.5**~5 ~5**  2.5**~5** 2.5 2.5 2
.5 2.4 

### 2.' 2.5 2.5 

### 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 

### 2.' 

## 2.' 2.' 0.99 1.00 1,02 1,02**0.9~** 0.97 0.9.3 0." 0.99

\.01 1.03 1.04 106 I ,CS 125 125 124 12. 12. 125 125 125 12' 124 12
.. 125 125 125 125 125 1 20 126 125 12. 125 126 125 125**l~o** 125 125 125 125 125 125 125 125 12' 125 125 125 124**12~ 12~**  

### 124 125 125 125 125 125 124 124 12
.. 125 125 1 25 125 124 12 • 124 12' 124 12' 12' 

### 12' 125 12' 124 124 124 124 Com.-r.ools



### Anatyzer CaHxation 

### Syslem 

### B6as Olitl Check**15-:.: '~** A oco: !iOO D..1l3. 15- rr rute av erag e5 

# I STACK A- inputs STACK B- inputs STACK C- inputs STACK D- inputs TOA5 NOx C EMS CA1OC<l 47S9 =llCOO.5:d.oe T<:JbIe 15**TI ~_l** **E ST** A!,'P RE COR D .1tP rc:i:;_A\rTmp_F _Al3laticP**vg 02~** **yg(** ):m2_ Avg (1JrAow 1

_ A v<TrTlp_F _Av 302.-Avg(1**02_Avg(2}::02~vg(2 .i** **fF1O'H2_Av:TrT:p_F** 

### _A v S02.:AYQ(1**~)'** 

# "" .f.", ,vs 0:2.. Avg(1**02_Avg(4)~02_Ayg(4.irFlow4_Av.:kTm -p_F**  _A vg (4 ) T S 

### AN I1HJ 

### DogF inH20 

### ppmD "I PrcntO ry PcntDry**H20** 

### O
.. F ppmDry PlcnlDry PcntOry n H20 

### DogF ppmO<y P=tO<y PcntO "I 

### ril20 DogF ppmDry PrcntDry PcnIDry <>H 2O 

### OogF A vg AV9 Avg 

### A"" A "" A VO A "" AVO AVO A,.**A'~** 

### A,. A"" A AVO A,. A"" A,. A , . 

# e.mm.n " 3/ 18'-08 11 :30 "'2 2c3.06 31 -0.16 6. ' 19A 1.2 OSS n 4 5.2 lU 

### t.e 0.83 110 I nva'td data 17.7 

# I.' O
. SO 117 

## s.a 17.9 2.4 1. 03 124 311 1).'

08 

### " : 45 463 28.06 31 -0.15 6.2 1904 1.3 0.83 11 3 '
. 7 18.9 1.. 0.85 110 lnvaid dala 17.7 

# . .• 0
. 83 117 3. 1 17.9 2.4 1.04 12.. 3' 18l08 12:00 

### 4G4 :<:a.07 29 -0.15 6.7 19.5 1. 2 0 .80 112 5 .1 18.9 

# ... 0.84 110 Invalid da b. 17.7 

# . .. 

# - 11 6 3 .4 17.9 2.' 1.03 124

... 5 :<:0.07 30 -0.15 6.7 19 ,5 1.3 0.58 11 2 5.2 18.9 

# ... 0.84 110 Invaid data 18.6 

### i» 0
. 82 11 7 3.4 17.9 2.' 1.05 12.. 3' l B1OS 1 2: 30 

# .... 2a.C3 29 -0 .15 6.3 1 9,5 1.2 0.86 11 3 4
. 9 18.9 

# I.' 0.84 110 l rwaltcl da ta 18.6 

# . .• 0
. 82 11 6 3 .6 17.9 2.' 1.03 123 3/ 1 &'08 1 2; 4.,5
... 7 28.07 30 -0 .14 6.1 19 ,5 

### t.z 

# o.sa 

# ' " 4 .5 18.9 

# . ,. 0.84 111 l nvaid da b 18.6 

# I.' 0
. 8 1 117 3. 3 17.9 2.' 1.03 124 31HI

/08 13 : 00 ... 9 28.08 31 -0. 14 5.9 19.5 1.2 0 .87 113 4 .5 18.9 

## t.e 0.83 III I nv aliddaU 18.6 

# . ,. 083 117 3.0 11.9 2.4 1.03 1 2
... 

### 021 C O2 

### MOIled 10Sll:lcl\B 3/ 160

' 08 1 3 : 15 

# .... ss.ce 31 -0. 15 6.4 19.5 1.2 0 .B6 113 5
. 1 '9.2 1.5 0.83 III InwIJd d ata 18.6 

# I. , 0 .82 11 7 3 .3 17.9 2.4 1,0 ... 1 £5 3/ 18.'08 1 3 : 30 470 28.08 32 -0. 15 6 .3 19 .5 1.2 0 .88 112 5 .3 1 9 . ' 1. 5 0 .05 111**d a t3**  18.6 

# . .• 0 .81 117 3 .2 17.9 2.4 1,0... 1 24 3/ 1&

'08 1):<15 

### 471 28.0 7 32

-0.15 6 .6 19 .5 1.2 0 .87 113 5 .7 \ 9. 1 1 .5 0. 84 11 1 lr"Mlt ddal a 18.6 

# . ,. 0 .83 11 6 3.7 17.9 2.4 1 .03 1 24 3o 't&'08 14 :00 472 20 .06 31 -0. 14 6.7 19.5 1.2 0. 87 n' 

# s.a 19 .2 1.4 0. 84 112 InYal d dal a 18.6 

### is 0 .82 117
.. .0 17.9 2.4 1.04 1 24 3 ' 1&

'081 4 : t5 473 2cl06 31 -0. 14 6.5 19.5 1
.2 0. 88 113 5.6 19 .1 1.5 0. 64 112 !nvaid ca ta 18.6 

# . .• 0 .82 117 3.9 17.9 2.4 1. 03 1 24 J,r l6- 'C

B 1 4 :30 

### 474 28
.05 30 ·0. 14 5.3 19.5 1.2 0
. B7 112 5 .4 1 9
. 1 1. 5 0. B4 1\2 I n VlWj da ta 18.6 

# . ,. 0 .82 117 3. 7 17.9 2.4 1.04 1 24 30 ' 18.08 t 4 :45 475 28 .05 31
-0
. 15 6 2 19.5 1.2 0 .87 11 3 5
.2 1 9 .1 1. 5 0
. 84 112 Invalid da: .a. 18.6 

# . ,. 0.82 117 3.5 f7 .9 2.4 1. 03 12
.. 3.' 1&'08 15 :00 476 23 .04 31 -0
. 15 6 .1 19.5 1.2 0. 88 

# "' 5 .2 1 9.1 1. 5 0.64 112 Invalid dat a 18.6 

# . ,. 0 .82 117 3.-=' 17.9 2. 4 1. 02 124 3.' 1 &'08 t 5 : 15 

## at 23 .05 3 1 -0
. 15 6 .3 19.5 1.2 0. 87 113 5 .3 19 .1 1. 5 0 .64 112 

# """"' dal
. 18 .6 

# . ,. 0 .82 117 3.5 17.9 2.4 1. 03 125 3i 16iOB 1 5 : 30 47.**~3 05**  31 -0 .1 5 6 .8 19 .5 1.2 0
. " 113 5 8 1 9.1 1 5 0.64 112 

# -- 18 .6 

# . .. 0 ,82 117 3 .9 ' 7.9 2.4 1.04 124 3.'l S'-08 1 5 :<l3 47. U .C S 31 -0 .16 6 .7 19 .5 1.2 0
. 58 112 5
. a 1 9. 1 1. 5 

## o.ss 112 invalid data 1 8.6 

# . ,. 0 .62 1\ 7 4 .0 17.9 2.4 1.04 . 24 31 1&"08 1 6 :00 

### 49::> 23 .00 3 1 -0 .17 7
. 0 19.5 1.2 0 .87 113 5 .' 1 9 .1 1 .5 O .g..; 112 

# """"'- ' 6.. 

# . .• os: 117 3 .' f7.9 2. 4 1.03 ' 24 31 1 8.03 16 : 15 

# "" :23 .06 31 -0 .17 7 .0 19 .5 1.2 0
. 87 113 5 .' 1 9 .1 1
. 5 

## o.as 11 2 

# """"dal
. 18.6 

### I.' 0
. 82 117 3.7 17.9 2. 4 1.03 '25 311&08 16 : 30 ... 2 28 07 31 -0 .17 7 .5 19.5 1.2 086 11 3 6 .' '92 1
. .. 0 .84 11 2 

# """" do '" •6., 

# . .• 0 .81 117 4
. .. 17.9 2. 4 1.0 3 124 3i 1&Da 16 :45 

### 483 20. 07 32 -0 .17 6 .' 19 .5 1.2 0 .87 113 5 .8 1 9.2 1 5 

## o.ss 11 2 Invaliddal a 16.. 

### I.' 0 .81 117 3.7 1 1.9 2.4 1.04 1 25 J,I,8.na 17 :00 

### 464 13 .07 31 -0 .17 7
. 1 19.5 1.2 0. 58 113 6 .0 192 1 .4 0.80 11 1 

# """" - '8 .6 

# . ,. 0
. 82 116 .. .0 17.9 2.4 1.04 124 J,!18!OE! 17 :15 ... 5 2e .07 31 -0.17 7.8 19 .5 1.2 0
. 87 11 3 66 19.2 1 .4 O.SS 11 1 

# """"dal
. 16.. 

### I .' 0 .8 1 11 6 4
. 5 1 1_9 2. . 1.03 124 311&"08 1 7 :30 

# .... za.or 31 -0.17 7.9 

## ts.s 1.2 0. 87 

# " ' 6. 19.2 1.5 0.84 112 Inv*fdal a '8 .6 

### I., 0.8 1 11 6
.. .7 1 1 .9 2. 4 1. 03 1 24 02 

### JCO2 ' .4O'II ed to Stack C 3/18108 

### 17:45
...7 za .07 31 -0.1 5 a.' 19.5 1.2 0. 87 

# "' 72 19.2 1.5 0 .94 112 In'rohd data 18
. 6 

### I .' 0
. 8 t 11 6 5 .5 17 .9 2.4 1.03 1 23

181 1 , 

# .... 28 .07 31 -0.1 5 

## s.o 19 .5 1.2 0 .a7 113 3,0 1 9.2 1.5 

### o.ss 1 11 

# .... i
. 0 8 0. 82 116 6 .1 17.9 2.4 1. 0 3 122 

### AtetSirVic. 3f181081l1 1 5 

# ...., 28 .07 32

-0.17 

## e.o 19.5 1.2 0 .86 11';' 7
.0 1 9.2 1.5 0.83 112 nvakl data 18. 6 1 .9 0 .83 116 

# ., 17.9 2.4 1. 03 129 3/t& '0818:3O 

## m 28.07 31
-0.19 

# rs 19 .5 •.2 0 .87 113 6 .' 1 9.2 1.5 0. 84 112 Invah :lda la 18.5 2 .0 0 .62 116 5.7 ' 7.9 2.4 1
.04 129 3/18108 18 : 45 491 28.09 31
-0.19 6.4 19.5 1.2 0 .86 113 72 7 9.2 1.5 0. 63 11 2 Invafid d a ta 18.6 

### I.' 0 .81 116 6 .0 17.9 2.4 1
.03 1 23 

### 02 l CQ2 M oved 

### to $tacll 0 311S '081 9:00 

# .., 28.C9 30 -0.19 82 '9.5 1.2 OSS 114 71 19 .2 1.5 0. 63 112 Invaf.d w ta 16.
. 

### I., O.Sl 116 5.8 17.9 2.4 1. 03 124 3o '1S ' C.a 19:15 

### 493 20.08 30 -0.19 7.9 19.5 1.2 0
.. 11 2 6 .7 19 .2 1.5 084 112 \nval.d da l3 18.6 

# I .' 0. 82 116 5.3 1 7.9 2,.;. 1 ,03 1 24 3.'1&'08 19:30 494 28 .06 29 -0.19 

## s.z 19 .5 1.2 0" 112 7 .1 19 .2 1.5 0 ,84 III 1nvahd da la 18.6 

# . .• 0 .82 116 6.0 1 7.9 2 ";' 1.04 1 23 30'1S

iCS 1 9:45 4 95 28.09 30 -0.20 7.7 19,5 1.2 0.8 7 11 2 6.6 19.2 '.5 0.84 112 inva!!d dal a 18.6 

### I ,' 0
. 84 11 6 5.' 17 .9 2 .5 1.04 .24 3/1&'08 20:00 496 28.C9 30 -0,20 

## e.o 19.5 1.2 0.S7 112 6.' 19.2 1.5 0.84 111 inva:id da l3 18.6 

### I ,' 0 .84 116 

## s.a 17 .9 2.5 1.04 1 23 3o'la '-C820; l 5 49 7 28.09 28 -0,20 7.7 19.5 1.2 0.86 11 2 6.9 '9.2 1.5 0.84 111 invalid dat a t8 .6 

# ... 0 .84 11 5 6,.;. 17.9 2.5 1. 03 122 3/ 1a:C8:<:O-.30 4 '" 20.\0 27 -0.20 74 19.5 ' .2 0. S7 

# " ' 6.5 '9 .2 1.5 0.84 111 inv alid data 18.6 

# . .. 0 .83 11 5 5 .6 17.9 2.5 1.03 122 3' laos 20; 45 493 28. 10 '7 -0.20 7a 19.5 1.2 0.B7 

### 113 6 .7 19 .2 '.5 0.84 110 Irrva:idda ta '6.' 

### I ,' 0.64 11 5 5 .5 17.9 2.5 1.04 1 22 3.'ls. '09:2 1 :C-:) 

### 500 28. 10 30 -0.20 7.1 19.5 1.2 0." 11 5 6 . 1 19.2 1.5 0.63 

# "' Inva.'id cata 18.6 

### I ,' 0.64 

## u s 4.6 17.9 2.5 1. 04- 125 3/ 18'-082 ' : 15 

### 50' 28. 10 31 -0 .20 6.9 19.5 1.2 0.87 \16 5 .' 

### 19.2 1.5 0.84 \14 !nvaid data t8.6 

### I ,' 0 .64 11 9 4 .' lBO 2.':- 1.04 12" 3/ 18.082 ' :3:) 

### 50' 28. 10 30 -0.2 0 72 19.5 1.2 O.SS \17 6 .0 19 .2 1.5 0.62 114 lIwaid data 18.6 

## t.s 0.82 1 2O 

## as 10.0 2.4 1.03 1 27 3/ 1S.

'0821 ;4,5 

### 503 28
. 10 31 -0. 20 6' 19.5 1.2 0 .87 \16 5
. 1 19 .2 1.5 0.83 114 lnvald da ta. 18.6 

# I., 0.63 

### " 9 ' .7 10.0 Z4 1.04 

### 127 3.' 1 

## a'08 22 :00 

### S04 28
. 10 31 -0.20 6. 1 19.5 1.2 0 .85 11 5 4 .9 19 .2 1.5 064 

## na I no-r.Ik:lda ta 18.6 

# I .' 0.82 11 9 2.5 lB.O 

## z.a 1.03 

### 127 3"-18

' 08 22 : 15 

### S05 28
. 10 31 ·0. 18 5 .B 19.5 1.2 0 .85 11 5 4. 6 19.2 1.5 0. B2 113 Inv alid dal.l 18.8 

# . .• 0 .S1 1 19 2 .4 18.0 

## z.a 1.03 127 3.'1 &

'0622: 3 ;) 

### SOO 28
. 10 31
-0 .18 5 .6 19.5 1.2 0 .S7 116 4
.5 19.2 1.5 0. 82 113 In\'.ud data 18.6 

# . .• O.S l 119 ' 5 18.0 2.3 1 .04- 127 3.'1 810822; 45 507 28
. 1 0 31 -0. 19 5 .6 19.5 1.2 0. S7 115 4
.5 1 9.2 1.5 0. 83 

# " ' invalid d ata. 7 8.6 

# . ,. 0 .S1 11 9 '. 6 16.0 

# " 1.04 127 3,'18 ;C8 23 :00 

# see 20.1 0 31 -0.20 5.' 19.5 1.2 0 ." 11 4 4 .3 19.2 1.5 0. 84 11 3 1nvaIP;j dala 18.8 

# I .' 082 1 19 2.3 18 .0 

# " 1 .CS 1 26 3.'IS ·0823 : 15 509 U .l1 30 -0 , 19 5 .0 19.5 1.2 OS7 11 4 4
. 1 1 9.2 1,5 0.64 

# '" InvaJd d :lta 18.6 

## ts 0
. 82 119 2' 18 .0 24 1 .C5 127 3/ t8.0823 :3O 5 10 

# za.n 30 -0
. 19 5 .0 19.5 1.2 0 8 7 11.. 4 .3 '9 .2 1 .5 0.63 ' 13 Ifflalid dau 7 8.6 

# I ,' 0 .94 119 25 18 .0 2 .' 1 .07 127 3. 'l &'CS 23 :45 511 :2 3 .1 1 30 

# -o.ao 4 .' 19.5 1
.2 0 88 11';' 4 .':' 19.2 1.5 0 .B5 113 1rIv3I d d ata 18.6 

### I .' 0 .94 118 '0 18 .0 2 .3 1. 06 125 31i QrC80:00 5 12 23 .12 '0 -0 .20 5.7 19.5 1.2 0 .87 It -=' 4
.6 19 .2 1.5 0
. 85 113 invalid d ata 1S .6 

### I .' 064 

# "' 30 1 8.0 2. 3 1. 05 1 26 3i l SWC8 0: 15 513 2& .12 

## a -020 5 .2 '9.5 '
. 2 0
. 88 114 4
. 1 19.2 1.5 0 .94 113 InvaIK:l da:.a 16.. 

# . .. 0 .85 118 2 .5 1 8 .1 2. 3 1 ,C5 126 31 ' '''''08 0: 30 514 28
. 12 2a -0 .2 1 .. 3 19.5 1.2 0 ." 1 1': 3 .4 1 9.2 1.5 0. 64 113 

# - - 18.6 

### I ,' 0 .94 119 1.7 1 8
. 1 2' 1.00 127 3 .'1 tw8 0:45 515 26 .12 

## aa -0 .2 1 3 ... 19 .5 1. 2 0 ." 11 3 2.5 J9.2 1.5 0 .63 113 InvaIId da: a 18.6 

# . ,. 083 11. 1 2 I B
.O 2 .' 1 ,C 5 12 8 3 !1Q108 1:00 516 23 .12 2a -0 .2 1 

## aa 19
.5 1.2 0
. 87 11 2 2 ' 

### 19 .2 1.5 O .SS 

# '" I nvalid da ta 16.. 

# . .• 0
. 84 11 8 11 18 .0 2 .3 1 ,0 5 127 

## v rece 1: 15 5 17 :<:8
. 12 

## za -0 .2 1 37 19 .5 1.2 O .s.: 113 2.8 " .2 1,5 0 .82 113 lnvaId di!1a 16.. 

# I., 0 .83 11 8 1.3 18 .1 2.3 1.04 127 3o · , WOS 1 : 3.') 51a 28
. 13 

### zt -0.2 1 2.8 19.5 1.2 0
. 87 112 2.1 19.2 1
. 5 

### o.es 112 InvaIid dala 18.6 

# . .• 0 .80 11 8 1. 0 1 8 .t 2 .3 1.07 1 20 3' l S1.'OO 1 : 45 5 19 

## eaia zt -02' 3 .0 19 .5 1.2 0 .87 

# " ' 2.4 1 9.2 1.5 O .SS 113 lnvahd d.1 t<2 16.. 

### I., 0 .8 5 11 8 1.1 l SI 2 .3 I. CS 1'Zl 3/ , g,;oe 2 00 

# '20 28 .13 27 -0 ,21 '5 19 .5 1.2 0 .88 11 1 2
. 1 19.2 1.5 0 ." 112 Invalid data 16.' 

### I ,' 0 ." 

## n e 1.1 1 8 .1 2 .3 1.06 1'Zl 3/1 g,.oa2;l5 521 23
. 14 27 -0.22 33 19 .5 1.2 0 .87 112 1
. 7 19.2 1.5 0 .58 112 Imalod
.... 18.6 

### I ,' 

## o.s s 11 8 1.0 1 8
. 1 2 .3 1.0 6 1 20 3/1 g,«)92 :30 '22 2a .''':' 26 -0. 22 '.1 19.5 ' .2 0 87 11 2 1 .7 19.2 1.5 0 ." 112 lnvahd data 18.6 

# I., O. e S 11a 0
. ' 10 _1 2.3 '. 05 1 2 7 3/1 W082:45 523 20 .\3 27 -022 2. 6 19 .5 1. 2 0 .S9 1 \1 1,4 19,2 1.5 0.89 112 lnvaliddal a 16.6 

### I .' 0 .87 117 0. 9 1 8 .1 2 .3 1. e9 126**3/1 ~3** **:00** 524 23 .13 :26 -0. 22 3 .3 19.5 1.2 0 ." \12 1.9 1 92 1.5 0.88 113 In vatid da t3 18.6 

# . , . 0 .6£ 118 1 .0 lil
. 1 2.3 1.0 7 1 26 3.' 1 ""003 : 15 525 26 .13 '6 -0. 22 

## a.s 19 .5 1. 2 0 .9 1 110 1. 5 ' 9.2 1.5 092 112 :m"3l idd.lta 18.6 

# . .. 008 117 0 .9 1 8.0 2.3 1.09 125 3/ 1 91063 :30 526 28. 12 ' 6 -0 .22 

## s.s 19 .5 .2 087 11 2 2 .0 19.2 1.5 0. <;0 1 12 lnvalid da ta 18.6 

### I ,' 0 .&6 l1 a 1. 2 'S.1 '.3 1
.06 12 5**3: 1~** **"oe3:4.5** 527 28.12 

### a s -0 .22 2.' '9. 5 1.2 

## o.se 11 ' 1 .5 19.2 1.5 0. 91 

## u a In valid dal a 18.6 

# . ,. 087 ". 0 .9 18.0 23 1.07 1 26 3/1 Qt{:S 4:00 52a 23.12 25 -0.22 3.4 19.5 ' .2 OS7 113 1 , 7 '9 .2 1.5 0 ,91 112 

### kwaI .d d ata 18.6 

# I .' 0 .87 

## ue 1.0 18.1 2.' 1 .05 12 5**3,'1 ~g,** **4: 15**  529 20. 12 25 -0.22 3.5 19.5 1.2 058 113 1.7 19 .2 1. 5 0.<;0 112 

# """"' - te» 

# I .' o.se ns 1.2 lB.l ' .2 I.C-6 125 3,'l WOS4:30 

### 530 28. 12 

# " -0.22 2.8 19.5 1.2 

## o.ss ' 12 

### 12 19.2 '.5 O.SO 

# '" lnva!id da ta 16.' 

### I .' 0 .3 7 "a 0.9 18.0 2.3 1 ,09 

# ' " 311W084 :45 5 31 23. 11 25 -0.22 2.5 19.5 '.2 osa 113 1 .0 19.2 1.5 0.92 112 Invalid da 13 18.6 

# I.' Oa7 

### tt s 0.8 lB. O 23 '.08 126 J.l 1 91'085.00 83' 2 8. 11 25 -0.22 2.8 19.5 1.2 0 .89 

### '13 1.1 19.2 1.5 0.91 113 In valiidda fa 16.' 

# I ,' 0 .88 " a 0.9 lo .1 2.2 '.07 ' 26 J.l1 WC85: 15 533 2312 25 -0.22 3.6 19.5 1.2 088 "4 1.1 19.2 1.5 0,91 "3 lnvaIIddata 18.6 1 .' 0 .58 " a 1.2 10.1 ' .2 1.08 126 3,'1 9i085 :30 534 2a.12 2 5 -0.22 3.5 19.5 1.2 0.S7 11
.. 1.
. 19.2 1.5 0.<;0 

# '" InvaIod dal, 18.8 

# . .. 0.87 " a I.' 18.1 2.' 1 .07 

## ias J.l1 1WC85:45 535 20. 12 2 5 -0.22 3.4 19.5 1.2 0 .B9 11 4 1.1 19 .2 '.5 0<;0 "2 In v<U ,d data 1&. 

# I .' o.se " a 1.0 10.1 2.2 I.OS 120 J.l 1Q-'

CS 6:00 

### 536 23. 12 2 4 -0.22 ,.4 19.5 1.2 0.87 115 1. 0 19 .2 1.5 0.B9 

# '" lnvaid dat a 18.6 

# I.' 0.87 " a 1.0 lB.l 22 

### ' .05 126 3I1 9r'C86 :15 537 20
. '3 2 4 -0. 22 3.' 19 .5 1.2 0." 

### 115 0 .' '9.2 1.5 0.B9 

# '" Inv*:! dat a 16.6 

# . .• 0.B5 11 9 

## o.s 18.' 2.2 1.06 127 J i1 g,.'

C8 6 :30 

## sss 2a. 13 24 -0.23 2 .7 19 .5 12 087 11 4 0.7 '9.2 1.5 0 .89 "3 Jnva! d o:iala 18.8 1 .' 0,87 119 0.7 18.1 2 .2 1. 06 127 J.l1 W08 6 :45 539 2a. 14 25

- 023 '. 4 19.5 ' .2 0 .S7 

# "' 1 .5 19.2 1.5 0 .91 112 lnvaIld data 18.8 

# I .' 0, B7 "9 o.a 1 0.0 2.' 1, 07 1 27

Pagl!8 TOA5**TI~.lEST .~P**  TS 3/18,"0811:30 

### 3Jls.'Oa " ( 45 3 / 1 &10 812 :00 3f l B1oe 1 2: 30 3/ 1 at06 12:4.5 3/18108 13 :00 3118108 13 :1 5 3118J08 1 3:30 3/1S/08 1) :<15 3H S"

08 14 :00 3 ' 1 8.' 08 14:15 3JI S;CS14 :SO**J. H~** **08** 14:45 31 1

81 08 15 :00 31 1

8108 1 5: 1

5 

### 3118108 15 : 30 J.' IS':oa 15 :<15 

### 3118."C8 1 6 :oo 3f lS : oa 1 6 : 15 3f1 8. ·

oa 16:30

3118.10819:00 J. ' 18.'C.a19: 1S 3!18.'CB 19:30 J.·lSic.g 1 9: 4.5 3/HYCB 20:00 J.'la' CS2O:1S 3/1a:CS20".30 3 ' 1ac-s 20:4.5 l'I8;'0921 :C') 3118"'0921:15 3118.0821:3) 3/Ia.:0821:4.5 3!1 Si08 22 :00 3':18'0822:15 3,11 6106 22:3 :) 3.'1 8108 22:45 3,11 IVCS 23 :00 J.'HJJCS23 ) 15 31 18.'08 23:30 3. ' 18108 23:4.5 3Ij QiC8 0 :00 Jl lWC8C: 15 31 tW'CS O: 30 3.'1 9108 0 :45 J.' t WOS 1: 00 1I1 W08 1:15**:l/ :30**  31 1W08 1:4.5 1'1 9r108 2:oo 311 g,1()8 2 : IS 1 ' 1 g{()9 2:3O 311 WOS 2:45 31 1 Q1Q8 3 :00**3/1 093:1S**  311 9108 3 : 30 3.'1S

lQ83:4.5 3il wt S4:00 3il Ml S 4 : 1S l'1 IWS4:3Q 3I1 WOS ·HS l'1 WOS 5
.C-o l' 1 11t08 5:1S 3.'1 91085:30 1'1 g,.'C 85:4.5 31 1QiCS6 :00 l'1 9r08 6: 1 5 3!1 WC8 6:30 3/1 WOS 6:45 Aoco:dOld Dal3. 1S- mirlute averages 

# I STACK A- 

### inputs STACK B- 

### inputs STACK C- 

### inputs STACK D- inputs

# NAo;C~~·~S**<lr~~~~~\rT:;~~ _A~'=~~'** **vg 1** **~~; ,** **)~ Avg(** **IJrAow v<** **mp_ F** _A
....

# ~A"g{l**02_A'I9(2P02.-Avg{2 .ir** **Aa.v2_Av:Trf..p_F_A V;** **:!IiI~~1lIq;1iI** AN l"IHJ Deg F inH20 ppmO ry PIenta ", Penl0ry i'1H20 Oeg F ppmOry PrcnlOry PcntOry n H20 Deg F



### 47. 475 

# "6 m

482 

# ... ... 485 

# .... 487 

# ... .... :.91 

### 492 

### ' 93 

# ' 9

' '95 '96 

### 497 

# 4" 

# ,,, 500 SO, S02 S03 

### se, se5 SC<6 

### 507 508 509 51 0 511 51 2 5'3 

### 514 

### 515 516 8 ' 7 

# "8 5 19 

# '20 521 

# '22 523 

### 524 525 S26 527 52. 529 

### S30 53, 532 533 

### 534 535 53S 537 538 53' 

# - -**~** 

# -**~** 

# - - - - 

# - - - - 2el06 31 -0.16 B.g 19.4 1.2 0,85 5
.2 1119 1.6 0.83 110 

### 28.00 31 -0.15 6.2 19.4 1.3 0.83 113 :. .7 18.9 1.6 0.85 110 2a.07 23 ..0.15 6.7 19.5 1.2 0.80 11 2 5
. 1 18.9 1.6 0.84 110 :2.a.07 30 ..0.15 6.7 19,5 1.3 0.88 112 5
. 2 IB.9 1.6 0.84 110 2a.C3 29 ..0.15 6.3 19,5 1.2 0.86 113 4
. 9 1B.9 1.6 0.84 110 28.07 30 ..0.14 6.1 19 ,5 j.2 0.58 113 4
. 6 18
. 9 1,6 0.84 111 28
.08 31 ..0.14 5.9 19.5 1.2 0.87 113 4
. 5 18.9 1.6 0.83 111 28
.08 3 1 ..0.15 6.4 19.5 1.2 0.86 11 3 5.1 '9.2 1.5 0.83 III 20.08 32 ..0.15 6.3 19.5 1.2 0.88 112 5.3 19.1 1.5 0.05 III 28.07 32 -0.15 6.6 19.5 1.2 0.87 113 5.7 19.1 1.5 0.84 III 20.06 31 ..0. 14 6.7 19.5 1.2 0.07 113 5.8 19.2 1.4 0.84 112 20
.06 3 1 · 0. 14 6.5 t9.5 1.2 0.88 113 5.6 19.1 1.5 0.84 112 28
.05 30 ·0.14 6.3 19.5 1.2 0
. 87 112 5.4 19.1 1 .5 0. 84 1 12 28.05 31 -0.15 6 .2 19.5 1.2 0.87 113 5.2 19.1 1.5 0. 84 112 20.0.; 3 1 ..0. 15 0
. 1 19.5 1.2 0 .88 113 5.2 1 9. 1 1. 5 0.84 112 20
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'0812.45 563 28 , 19 27 -o2J 4 .9 19.4 1.4 O
. SoJ 11 1 3 .9 19 .2 

### r . 0
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# I .' 0 .35 116 2
. 3 18.1 2 .3 

### '06 l Z" '1' 19 'C813 :0 J 584 28
. 19 29 -0
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# I .' 0 .85 115 2 4 '8.1 2 .3 

### '06 ' 23**19.0B** 13 : 15 50S 28
. 19 32 -ON 5 .3 19.4 1.4 0 .9') 110 4
.3 1 9. 2 1 .5 0. 87 109 lnvalid dl la '8.6 

# I.' 0
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### ' 06 ' 23 31 19"08 J 3 : 30 588 28
. 19 34 

## -o.zo 5 .4 

### lU 1.4**.~** 111 4
.4 1 9 2 ' 5 0. 89 1 09 lnvaid data '8.6 1 .' 0
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### V 18.1 2 .3 

### '06 123 31 1Q.

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# I
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### l a S 

# f.' 115**~9** 

### lal 2
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# , """'- 18
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# f.' 0
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# zs 18
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. 8 

# I .' 0 .84 11 5 

## z. s l a l 2 .3 

## us 123 3/1910814;30 570 28 , 18 38 · 0 .19 5 .' 19.4 1.4 0 .00 11 0 4.7 19_ 2 I.S 0
. 86 

### ,og**val' ~da**  18.6 

# f.' 0. 84 115 2
. 7 

### la l 2
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. 18 39
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# I .' 0. 88 11' 4.9 19 .2 I
. S 0 .96 ' 08 !nvaid da la 1 8.6 2 0 0. 83 ' 15 18
. 1 2
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# """" d "" 18 .6 2 .0 0.8 1 ' 15 28 18
. 1 2 .3 '04 123 3I l\} OO 15:15 573 2 8
. 18 39 -0.18 5.5 '9.4 1.4 0.8 9 

# "' 4 .5 19 .2 I.S 0. 97 ,C9 

# """" - 18 .6 2 0 0 .81 1 15 2. 18.1 2 .3 1.0 2 ' 23 3 /1Q.

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. 18 38 -0.18 5.' 19.4 

# I .' 0 .89 11' 4.0 19.2 I.S 1.0 ' 

# ,ea**data** 1 8
. 6 20 0.81 11 5 2
. 3 lS.1 2.3 '04 ' 23 3i l Q.

'08 '5:45 575 28 .18 39 -0.21 5.5 19.4 

# I .' 0. 93 ,C9 4.3 19.2 

### is 0 .92 !C9 Inva[ d data 1 8 ,6 2.0 0.80 '15 2.
.. 1S .1 23 '.02 ' 23 311

Q'C8 16:00 57' 28 .1 8 39 -0.23 5.4 19.4 

# I .' 0.90 107 4 .2 19.2 I.S 0 .95 lC9 lnvahddal<l 1 8
. 6 2.0 080 114 2 .5 1S.1 2.3 

### 1.03 1 23 3' 19.-'

C81 6 :15 5r7 28 .13 

# '" -0 .20 5 .8 19 .4 

# I .' 0 .97 '07 4 .5 19.2 I .S 0 .83 ,C9 

# """"" - 1 8
. 6 20 0. 00 114 2. ' 18.1 2.3 1.02 ' £'3 57 8 28 .19 

# '" -0 2 ' 5.5 19.4 1.4 0 .97 ,OS 4 .4 19.2 I .S 0. 90 110 lnvalid dal <.l 18 .6 2.0 

# - 114 2 7 IS
. 1 2.3 1.!}:) ' 23 31 1 W

OO 16; 45 579**19** 39
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### ' 03 4. 7 19.2 I .S 0
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# """"" - l 8
. S 2 .0 0 .76 115 2 .7 18.1 2.3 1.01 '23 3i l W09 17 :00 

# '50 28 ,'8 38 -0. 2 1 5 .' 19 .4 1.4 0 .97 107 4 .5 19.2 I .S 0 , 8 1 

### '03 

# , ,,.,.,. - ' 8 .S 2. 0 0. 76 11 4 18 .1 2 .3 '.01 122 3' 1 W06 17 : 15 58 1 28
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### 3'3 -0
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### o .se ,OS 5
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### 1.'" .23 31 1 9 '08 17 :3 :> 582 28
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. S 0 61 11 0 I nv .1.·ic1daIa 1 8 6 2. 0 0. 77 

### ' 16 2 .7 18.1 2 .3 

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. 79 ' 09 I nvaid data 1 8 ,6 0. 60 

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### ' .02 123 311 QlOS 1 8 :00 

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### 35

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.7 19.4 1.4 !C9 4.• 19
. 2 I .S 0 81 109 Inv3IIdd a t<:l 1 8
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. 1 2 .3 1 .0< 122 587 2 8 .21 30 -0 .22 •. 7 19.4 

# I
.' 0.9 8 ' C 9 5 

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. 2 I. S 0 .90 !C9 Inv»d da l <1 ,. 6 2 .0 0
. 85 1 14 3. 7 18. 1 2 .3 1
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### l a l 2 .3 1
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. 6 

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. 0 18.1 23 1
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# I .' 0 .97 IC9 5 .' 19.2 I.S 066 , C9 InwIId da ta 

### l a . 

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# I .' 0.97 'OS .. . 9 19
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### 3 5 18
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### 2.0 0.84 115 3 .2 

# ,. 0 2' ' .00 . 22 1119108 20:15 593 28 .24 25 -0.27 '.0 19.4 1.4 0. 93 '09 4.8 19.2 I.S 0 .91 110 

# """""' - l a . 

### 2. 0 0 .85 

### '16 3 .C 18 .1 2.6 1 .04 123 311Q.

' 0 820:30 594 28 .25 2. -0.28 

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### 2.0 0,05 

### '16 3. 0 18 .1 25 1.C5 124 1I1 g.ooa20:45 585 28 2. 24 -0.23 5.9 19.4 

# I .' 0.9 3 'OS 4 .9 19.2 I .S 0 .85 "'0 

# """"" - 18.6 

### 2.0 0.87 

### '16 3 .3 

## , a.l 2. 5 1.06 

### ' 22 3.'19' 0821 :CO 596 28 ,27 2 3 -0 .29 5 .9 19 .4 

# I .' 0.S8 'OS 4 .8 19 .2 I .S 0. 84 lOS 

# """"" - 18.6 

### 2.0 0.81 116 3.3 1 8 .0 25 1.COO ' 22 311 !K'1821 :t5 597 28
.27 21 -o.3- J 5 .8 19.4 1.4 0. 97 103 4.7 19.2 I .S 0. 83 'OS Invaiicl da la 16.6 

### 2.0 0.87 

# ,,, 3 .2 1 8
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! 06 2 1'30 598 23
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### 2.0 0 .86 ' 15 2
. '8 .1 2 .5 1.06 ' 22 3119'C8 2 1:45 

## ss 28 ,27 22 '() 2 8 4 .8 19 .4 1.4 0 ." lOS 3 .8 19. 2 I .S 0. 9 3 ' 09 I nvalid data 16 .6 

### 2 .0 0. 86 115 2 .5 18
. 1 2 5 1.CS ' 22 3i1 !W8 22 :00 600 28 .28 21 -0 .28 4 .6 19 .4 

# '" 0. " 1 08 3
.' 19 .2 I .S 1.0 7 ' OS I nvatd d<1 1.1 18 .6 

### 2
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. 1 2 ' 1.06 '22 3I 1 Q10822 : 15 60 1 28 .28 23 -0 2 7 4 .9 19 .4 1.4 0 .9 3 1 03 3
.' 19.2 I.S 1.1 2 110 I nvaid dat .1 18 .6 

### 2
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# , ,, 2 5 1 8 .\ 2. ' l.OS '23 31 1 9.'0622:3) 602 29
. 29 22 -0
.28 4.4 19
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. 4 1.0 1 108 3
. ' 192 I .S 1.0 3 11 0**d.11** 18.6 

### 2
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. 1 8 .0 2. 5 

### 1. 06 '22**g. '0822:.;s**  60 3 28 .29 

### 21 -0 .28 5 .3 19.4 

# I .' 0 .9 3 '08 4 .2 19
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### 2
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-0.29 5 .0 19.4 

# I
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### 2 0 0 .88 1 15 

# ze 18.0 2 

### .s 1.0 3 ' 22 311 !M'0823:15 

## scs 28 .3 ) 20 -0 29 5 .1 19.4 1.4 

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### la . 

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. 1 2. 6 1.0 7 ' 22 311 9 ,'0 8 23 : 30 605 28 .30 21
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### 20 0. 88 11. 18
. 1 26 1.0 7 122 

# , '45 60 7 28 .3 1 21

-0.30 4 .5 19.4 

# I.' 0. 99 

### ' 09 3. 19.2 I .S**C.** 110 lnvaid dala 

### la s 

### 2 .0 0
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# 80' 28 .3 1 20
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### '08 3.9 19 ,2 I.S 0.9 7 11 0 I nv<Od d3ta 1 S.6 

### 2 .0 0
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0 6 0 :15 809 Z a. 3 1 20
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### '09 4.0 19.2 I.S 

### 1.02 110 lnvUj da ta 18.6 

### 20 0 .87 11. 

### 24 1 8 .1 25 1
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### 2.0 0. 87 

# ,,6 2
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' 080:45 611 28 .32 '8 -0.3' 42 19.4 1.4 0
. 97 '07 33 19.2 I.S 1 .07 110 Inv aid d ala 1 S.6 

### 2 .0 0 ." '16 2 2 1 8 .1 2.' 1. 06 ' 23 3,1 2CVQ8 1 : 00 61 2 28 .32 17 -O..3J 3.9 19.4 1.4 O.Q !l 107 3.0 19.2 I. S 1.C'6 ,C9 I nvaid data 16.6 

### 2 .0 0.89 116 2. ' 

# '8 .' zs I.OS ' 23 .3 I2Or

"0 8 1:15 61 3 Zd.3 2 ' 7 -0.31 3.9 19.4 1.4 0.9 7 

# ,eo**~9** 19.2 I.S I.OS 109 InvakI da U 18. 6 

### 2.0 0." 1'5 

### 21 18 .1**~5** 1.07 ' 23 3 1 2008 1:30 614 28
. 33 

### 16 -0 .3 1 4 .9 19 .4 1.4 0 .9 5 '07 3 .7 19.2 I .S 1.11 

### '09 Inv aid da t.;) ' 8. 6 

### 20 0.89 ' 15 2 3 18 .1 25 '.07 '22 

### 3J2nI08 1 :45 615 28 .32 

# • •

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### 2 .0 0.89 ' 16 21 1 8
. 1 25 1.08 ' 23 61' ::8 .32 

# , .

-0.32 3.9 19 .4 1
. ' 0 .96 

### '09 30 19 .2 I.S LO t 112 In vaid d3l3 18.8 

### 2 .0 0.90 

# '18 1 ,5 1 8 .1 2 .5 1.07 125 3I2<M'08 2:1 5 617 28 .3 2 17 -0 .33 4.2 19 .4 1.4 0.95 , C9 3. 6 ".2 I .S 0 .81 11' 

# ."""' - 18 .6 

### 2
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. 8 1 8.2 2.4 '.OS 124

TOA5**TI~.~ESTAMP** TS**311 ~'** **08** 7:00 31 I WOO 7 :1 5 31 1 W08 7 :30 3119.108 7:45 311 9108 8:00 3f1 91C8 8 :1 5 Jll 9fC8 8 :30 31 19i08 8: 45 Jl1 9

':ce 9:00 Jl1 9{08 9 :15

311W0610:15 31 1Q/08 1O:30 3I 1W08 10:45 3I1 !)10811:00 30'1910811:15 311 9108 11 : 30 311 9108 1 1:45 3.'1 9108 12'.00 31H

VOS 12:15 311W0812:3-:) 3119108 12.45 311 9lC a 13:(}:) 3119;0813 : 15 3/1 90'08 13 :30 3119;0813:45 311Q.'U814 :OO 311gj()S 

### 14: 15 3/1910814;30**91Oe** 14:45 3I1 91Oe 15:00 3/19(00 15:15 3 11 9.'08 15:30 3I1 9(()8 15:45 lIHW08 16:00 311g.108 16:15 3I l !lJ0615;4S 311910S 17:00 311 W08 17 : 15 311 9108 17 :3 0 3-" 9108 17;45 311 9100 18 :00 311W08 18 : 15 311W0818:30 31H

W8 19:00**311!w 81~15** **3I 9108** **1~3O** 311 910819: 45 311 9J08 20:00 1'1 91OB20 :15 311 910 820:30 311 9108 20:45 311 9/08 21:CO 311 9108 21:15 311 9106 2l'30 311 9108 2 1:45 311 9108 22 :00 311 9J08 22 : 15 311 9108 Z2:3J 311 !W8 22;4S 3 11!)/(JS23 :vJ 311 1J08 23:15 

### 3I 1 91Q823: 3O

, 46 3I2OIOEI0: OO 3/2O{06 0:1s 3/201080:30 3120.'0 80:45 3/20108 1 : 00 2 t2Or'

061:1s 3 f2OlO8 1 :30 

# I STACK A- 

### inputs STACK 8- inputs Recorded**Ca~a** 1 5-mi"Me**ol'.'~~**



### STACK C- inputs

# NRo;C~ERP.~**S <l** **r;~'~~A\rT~;~: _Ail~~~~~~~2** **vg(1 ~:** **, ):02~** **vg( lJrAowl_** **AV( Tmp** **F**_Av502_AYa(1

# 02.-AIIg(2):02~vg(2JrF1ow2_Av:Tnip_F**-A Il** **"- ~iJ** **r- 0!~** **i?lipiiil11 ipiw:t~**  RN Intig 

### DC'9 F nH20 ppmOry P rc nlOry PI;ntOry inH:20 Oeg F ppmDry PrcnlDry Pcn10f'J in H20 Deg 

### F

# 2~**5 ~~g** **-~~:s ~~~** **~~ ~~** **~ ~~~** **~~ :~** **~'1 ~;~** **~~ !..-.·** **IiII~~~~~"' liii.iiiil** **it** 

# ,.., 542

550 55' 552 553 554 

### 555 556 557 558 559 560 56' So"2 563 565 566 567 568 569 570 57, 572 573 574 575 57' 

### 5r7 

# 51' 550 58, 5B2 583 584 585 586 587 5S6 589 590 59' 592 593 59-< 555 596 597 

# 5'" 59' 600 60 ' 602 603 

# "'5 606 607 

# 50' 509 610 611 612 613 614 '15 

# '16 617 2a,1G 25 -0.23 5
. 7 19.5 1.2 0.89 3.0 19.2 

### 1.5 0.91 I" 2a,1G 2 4 -0.23 5.4 19
. 5 ',2 O.BS 112 4
. 1 19.2 1.5**o.~** 110 28 ,16 23 -0.23 4.5 19
. 5 1.2 o.aa 112 3.3 19.2 1
. 5 0.91 11 0 [nvaliddala Zd.17 23 -0.23 4
. 8 19.5 1.2 0.8 7 112 3.6 19 ,2 1.5 0.91 11 0 Invaidd81a**~8.17** 2' -0
. 23 5
. [ 19.5 1.2 0.88 113 3.7 19
. 2 1.5 0.90 110 Inva£-dda:a 28_ 17 24 -0.£3 5 .3 19
. 4 1
. 4 0.88 113 3.9 '9
. 2 1
. 5 0 .89 111 28
. 17 24 -0
. 23 5
.6 1 9.5 1
. 3 0.87 113 4.2 19.2 1.5 0.89 110 28.17 24 -0.22 5. I 19.5 1.4 0.88 1 1 2 3 .9 19.2 1
. 5 0.90 1 \0 28.17 24 -022 5.2 19.4 1.4 0.68 110 3.8 19.2 1
. 5 0.95 110 InV1llddolla klvafiddata Inva(

d data I nd

.d data 2a.18 24 -0.22 

# ,.4 19.4 1.4 0.87 III 3.3 19.2 1.5 0.90 I tO Inva[d data 28.18 23 -021 4.7 19.4 1.4 0.89 110 3.5 19.2 1.5 0.96 110 Invafiddab 28..1S 23 -0.20 5.0 

### HI.S 1.3 0,90 11 1 3.7 19
.2 

### 1.5 1. 0 1 11 0 

### lnvalid daSa 28.1S 24 -0.21 5.7 19.4 1
. 4 0.91 111 4
. 2 19
. 2 1.5 0.96 110 I nvalid dill<l 28. 1S 2 4 -0.21 5.7 19.4 1,4 0.91 110 4.4 19
. 3 1
. 5 O.sa 110 Invald datil 28
. 1S 25 -0.21 5.5 19
.4 1.4 0.91 112 4.5 192 1
. 5 1.02 110 lnva5d dal3 28
. 1S 25 -0.21 5.1 19.4 1,4 0.00 110 ':.1 19 .2 1 ,5 0.84 110 Inv.tid data 28
. 1S 2Q -0.;:0 5.0 19.4 1,4 0.90 III 4.1 1 92 1 ,5 0.87 110 Invaid dal;;l 28.18 25 -0.20 4.9 19.4 1, 4 0.88 111 3.8 1 9.2 1.5 0.94 110 28. 1 9 26 -0.20 4.7 19.4 1.4 0.9 1 111 3.8 19.2 1.5 0.93 110 28.19 27 -O.@ 5.3 19.4 1
. 4 0.83 1 12 ':'.2 1 9.2 1.5 0.94 1 10 28
. 19 27 -0.£0 5.3 '9
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.2 1
. 8 0.79 110 28,19 27 -0.20 5.2 19
.4 '''' 0.89 111 4.2 1 9
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.23 4
.9 19
. 4 1.4 0. 5-;' 111 3 .9 19.2 1.6 0.9 4 103 28. 19 29 ·0
.20 5.0 19.4 1.4 0.9 1 110 4
. 1 192 I.S 0.9 3 109 28. 19 32 -0-20 5 .3 19
.4 1.4 O.9-J 1 10 4.3 19.2 '
. 5 0.87 109 [nvaid dat;). Invaid data Inv-Ud dal<l Invaid data InvaSd dallll**[~ ::!data**  Invaid d.lta Invaid dolla 28.19 3.:. -0.20 5 .4 Ul4 1.4**O.~J** 4.4 192 I.S 0.89 t 09 lnvaId data 28.19 36 -0.19 5.9 

### la" 1
. 4 0
. 89 4.8 19 .3 1. S 0. 68 1 09 [nv;Udd<lt<l 28.19 35 -0. 19 5.5 

### la4 1.4 0. 89 4.5 1 9
. 2 1.S**o.~** 1C3 Invaliddata 28.1a 36 -0.19 5.4 19
. 4 1.4 0.91 111 4
. 5 19.2 1.5 0.98 110 I nvaid dalO 28
. 18 38 -0.19 5.8 19.4 

### t.4 0.00 110 4.7 19.2 1
. 5 0.86 103 I n Vdf.Odata 28. 1 a 39 -0.19 6.2 19.4 1.4 0.88 1\1 4.9 19.2 1
. 5 0.96 lea 28
. 1a 3S -0.18 5.9 19
. 4 1.4 0.88 4.7 19
.2 1.5 0.95 108 28.1a 39 -0.18 s.B 19.4 1.4 0.89 111 4.5 19
.2 '
. 5 0.9 7 103 28
. 1S 38 -0.18 5.1 19.4 1,4 0
. 89 111 4.0 19.2 1.5 1.01 lC8 Invaiddata Invatd d"" Invatddab**~, data**  28. 1S 39 -0.21 5.5 19.4 1.4 0.93 109 4.3 19.2 1.5 0.92 lC3 Invai:d d ata 28 .1S 39 -0.23 5.4 19.4 1,4 0.90 107 4.2 19
.2 1
. 5 0
. 95 lC9 1nvaIIdda.t<J 28.19 .;0 -0.;:0 5.8 19.4 1,4 0.97 107 4.5 '9.2 1.5 0.33 109 InvaIidcbln 28 .1 9 .;0 -0.21 5.5 19
. 4 1,4 0.97 109 4.4 19..2 '
.5 0.90 110**~di:ltn** 2'8 , 1 9 39 -0.21 6.1 19.4 1.4 0.97 109 4.7 19..2 1.5 O.as 109 Invaiddala 28 , 18 38 -0.21 5.8 '9 .4 1,4 0.97 10 7 4.5 19.2 1
.5 0
. 8 1 109 I nvalid 

### daID. 28
. 18 3S -0 .2 1 6.4 '9
. 4 1.4 0 .\16 109 5. 0 19
.2 1.5 0.8 1 109 I nvaSd 

### data 29.18 38 -0.2 1 5 .8 19.4 1.4**o.~** 109 4.5 19.2 , .5 0 61 1 10 I nva'id data 29. 19 37 ·0.21 5 .2 19 ,4 

### 1-4 0.97 109 4
.2 19
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. 5 0. 79 109 I nvaid dala 28 20 35 -0
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. 5 0.69 110 6rrv8id d ata 28.23 25 -0.2.6 63 19.4 1.4 0.97 109 5.1 19
.2 1.5 0.66 109 28
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### STACK D- 

### inputs Avg(1 02.-A\'g(4POU\/Q(4.irF"1oW4_A>d.Tmp_F 

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02 I C O2 Moved to Stack B

02 1 CO2 MoIled to Stack C**I~P.\ i.,** FWcof dt!d l. 5-mnut:e**averag** 

# I STACK A- 

### inputs STACK B - 

### inputs STACK C · 

### inputs STACK 

### 0- input s TOA5 :-.rOx**CE.'.~S** CR 1roJ 4 789 =i 1000 .Sld
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### i .os res I nvalld dato. 18 .6 

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# """"' data te« Z O 0
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### res I rwaIldd ata 

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### laB 2.0 0
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### 1.t 2 ' 22 3/2Q,'Q 99: 45 647 26
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### t92 t.5 0.81 lCS 

### nvaLd 

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### 2.0 0. 90 11 4 3.5 l a l 2.' l C3 ' 22 3/2"'

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### 192 t.5 

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### 2.0 0 ." 115 3' lal 2 .' 110 122 31 2CJ08 1 0:15 64' 28 .40 14 ·0.33 B.3 i9.6 1.4 0.88 l C 9 6
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### t.5 0.78 l C3 ffl(d , :j 

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### t.5 0.82 l C3 ffla' j aal Q 18.6 

### 2.0 0 .87 11 5 3 .2 78.1 2 .' 

## i
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a 18.8 

### 2.0 0.87 115 2B 7S .1 2 .' t .07 123 

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### '46 2.0 0.8 7 115 3B 18.1 2.' 

## i
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### 19 -0 29 B.' 19.7 1 .3 0.93 

## n a 7 .3 19 .2 

### t.5 0.79 109 klvalid da l3 t8 .6 

### 2.0 0." 115 5.2 18.1 2.' 1
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## ics lnvalid da lJ 18 .8 

### 2.0 0 .8 7 115 4.B 18.1 2.' 1 .07 122 3i 2O'C8 12 :00 656 20.4 9 20 -0. 27 8.4 19.7 1 .3 005 11 2 6 .' 19.2 1.5 0.82 103 Irrva6id a.tla 18.6 

### 2.0 0. 85 115 4.6 18.1 

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### 21 -0 .26 B.B 19.7 1 .3 1 ,07 1 12 7
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### t.5 0.91 109 lnvajd d at3 

## ts» 2.0 0. 84 \15 4.' 18.1 2.' 

### l OS 1 22 3I2I:W8 1 2:10 6 58 28 .48 2 1 -0 .27 8 .6 19 .7 1
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### 2.0 0. 84 115 4.B 18.1 2.' 1. 07 122 31 201'0812:45 65 9 28.4 S 22 -0.20 8 .7 19.7 1.4 1. 02 112 

### Nccara 19.2 

### t.s 0 .95 107 28 18 .6 

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### 25 -0 .28 B.5 19.7 

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### 2 .0 0.82 liS 4.5 18.1 2 .8 1 .06 '22 31 2C.108 13:30 602 23 .47 32 ·a 2\3 B3 19.7 1.4 

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### Nc ca ta 1 9
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### 32 ·0 2\3 B.7 19 .7 7.4 

### U O 111 NodiUa 1 9
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### 2 .0 0 .63 114 U 18.1 2 .8 1
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### 2.0 0
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.4 112 Nodala 19.4 

### "2 No data 

### 19
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## '.5 1.6 1.5 0.84 0.83 0.66 0.a9 0.89 

## lea 107 107 107 107

Pa-ae 1 1 2
.a 18.1 

### 2.0 0.75 116 2.3 18.1 

### 2.0 0
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### 2.0 1B.1 

### 2.0 

## o.n ,,6 2.2 18.1 2.0 0.76 , 16 2.5 18.1 2.0 0.76 ,,5 I.' 1.. 2,1 2.0 

### I.' 1.. 1.8 1.8 1.S 2.1 2
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### 21 '.2 

# ,. IS 1.7 I.S 1.' 1B.2 1B.2 1B.2 1B.2 18
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### 182 182 lB.2 18.2 18.2 '8.2 

### 182 18.2 2.4 2.4 2.4 24 

### 2.4 2.4 2.4 2.4 2.4 2.4 2.4 2.4 2
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### 2.4 2.4 1.06 1.00 1.05 1.05 '.05 I.C5 1.05 1.04 1.05 1.05 U)' 1.04 U)3 1. 0 1 1
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# ," 122 122 122 123 123 123 123 122 System 

### ElIas On!! Check**eco~ t<:l**  Data 1 5- rTW'ul e averag H 

# I STACK A- inputs 

### STACK B- 

### inputs STACK C- 

### inputs STACK D- inputs TOAS ;..;0;.;**:. ~f:**  CR1 000 ..769 =llOOl Std
.C9 Tat : e 15**~E ST**  RECORD ar Pf ill'Ss

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_F**...Av~~A \.** **'Sl1 02_Avg** **(2 »)02~vg(2** **MFkw.'2..Av;TmP_F_A** 

## 1 1

# "" Y302- A\Ig(1**02_Ayg(4 )~vg** **(4.irfJcNJ4~V:kTmp_F** -Avg (4 j TS RN**~,.,** DL '9 F bH20 

### ppmD.., PrentDry PcntOry InH20 

### DogF ppmD.., PrcotDry PcnlDry <>H 2O 

### DogF 

## ..,..o.y f'1a>IDry

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### DogF ppmD.., Pn=r.IDry PQ1tDry i\H20 

### DogF A'9 

# A,. Avg A'9 A'9 A'9 A'9 A'9 A'9 

# A ,. A, .. A'9 A'9 A A A A A A'9 A'9 A'9 ''9 A'9 

### ccn-reots Ji21 /ca 17:20 

## m 28.43 30 -0 .26 5 .' 

### UJ.7 1.3 094 

### '09 No data '9.4 1.5 0 .88 ' 06 2. 8 18 .8 2.0 0.7 8 1 15 2 .0 18,2 2.4 1.03 1 21 Ji21iCa 17:45 775 28.43 29 · 0.27 5.2 19.7 1.3 0 .95 \09 Nc cata 19A 1.5 0.86 '06 2. I S,S 2.0 0.79 1 1'- 2 .' 18.2 2.4 1.03 '2' 3121iC918:0J 77 5 28.44 29 -0.2 7 4 .9 19.7 1.3 1.01 110 No cata 79.4 1.5 0.9 2 107 28 18
.S 2' 0.79 11 5 2 .0 lB2 2.4 

# ,"" , 22 3.'21i0918 :15 T77 28.44 28 · 0 27 5. 2 '9.7 '.3 0 ." 110 Ncoara '9.4 '.5 0. 85 107 30 18.S 2.0 0.81 115 2.' 18.2 2.4 

# l.('
. ' 22 3.'21'-03 1 8:30 778 28.44 27 · 0 28 5.7 19.7 1.3 0
. 97 11' No data 19.4 ' .5 0.8 5 107 3. 7 18.S 2.0 0.82 I1S 2.• 

### 18.2 2.4 

# ,'''' '2' 3 12 1;081 8:-+.5 779 28 .45 

## ze ·0 .29 5.0 '9.7 1.3 1.02 11' No data. 19.4 1.5 0.8 9 '07 3.7 18
. S 2.0 0.82 I1S 2
. ' 18.2 2.4 1 .05 '2' 3.' 2 1;03 19:00 780 28 .43 26 ·0 ,28 5. 3 19.7 1.3 103 110 No data 19.4 1.5 O.SO 107 3.9 l S.6 2.0 0.82 11 5 3.0 18.2 2.4 \.06 ' 2' 3.'2'''03 19 : 1S 7 " 28. 43 25 -0 ,28 6 .3 19.1 1.3 \. 05 11 ' N o dcra '9 .4 ' .5 O .SO 

### '06 3.' 1 8
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### -0 .28 6.0 19.1 1.3 0. " . 11 No data 

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### res 3 .5 18.8 2.' 0 .83 11 6 2 .5 18,2 2.4 t.CS ' 22 J,2 1Xl8 2Q:OO 764 213
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### 2.< 18.2 2 .' lOS ' 22 

## aavce 20: 15 7&5 2aA 7 23 -0 .28 6A 

### lH 1.3 1
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### res , . r 18 .9 2 .' 0.82 115 3.2 18.2 2.4 I
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### 'H 1.3 1 .00 11 

# xo eata 1 9.4 ' .5 0
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### rca 

# ,

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## n e 3 .5 18.2 2.4 1 06 "2 3. ' 21 J

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## as 28.48 

# " -0 .23 

## e. 3 19.7 1.3 1.03 1 11 

## xoceta 19 .4 1. 5 0.93 lOS 38 18.8 2 .' 0
.64 11. 3.2 16.2 2.6 1.06 ' 22 3. '21iC9 21:3O 

### 790 28. .:0 22 · 0.30 6. 1 19.7 '.3 0 .93 tt t No data J9.4 

## ' .5 0.89 108 3.7 18.8 2.' 0.85 11. 3.' 1 8.2 2.5 

## '
.06 '22 3.'21

i03 21:45 791 28." 22 -0 .30 6.3 19.7 1.3 1.00 

### u t No data 19,4 1.5 0.85 108 38 18.8 2.. 0. 85 

### '16 32 18. 2 25 '1. 06 '22 3i2110822:OV 792 26." 22 -030 5. 1 19.7 1.3 

### 1.a.: 

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## e. 2 19.7 1.3 

### 1.0-+ 

# ", No oa ta '9,4 1.5 0. 84 108 3.8 78 .8 2.1 0.85 11 . 3.3 182 2 .5 1.07 122 3.'21/

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# "' No cera 19.4 1.5 0. 87 

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# "' Nc 

## cata 19 .4 1.5 0.8 5 '03 3.7 18.8 2.1 0.65 11
. 3. ' 18.2 2.6 1 .07 '22 312 1' 08 23 : 15 797 28.50 23 · 0 ,30 6.2 19.7 1.3 0 ." 11' No data f9.4 1.5 0.86 '07 3.' 18.8 2 .' 0 .65 11
. 2. 18.2 2.5 1 .07 122 3.'21JC8 23 :30 793 28 .50 23 -0, 3:1 5 .8 19.7 1.3 0. 93 '11 No data**1~4** 1
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### res 32 18.8 2,1 0.35 115 2 ' 1 8.2 2 

## .s 1
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## ice 3 .' 18.8 2 . 1 0 .87 

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# " · 0.3 2 

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## r ca ' .0 18.8 2 .1 0 .89 116 3 .3 18.2 25 1. 09 ' 22 3. ' 22t03 0:-+5 

### 80J 23 .50 

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### i.ce 1 22 J,l 22JOB

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### res 40 18.8 2 .1 0.86 115 3. 1 8.2 25 1
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## l oa 3.9 18.8 2.1 0.68 115 28 18 ,9 2 .0 

### UO 121 

### FltwSeMCG J, '22ICO1:45 807 28.50 

### t e -0 .3 1 6. ' 19.7 1.3 083 11 3 

### xo cata 19 .4 1.5 0. 92 108 3.7 18.8 2.1 0 .86 ' 15 3 .4 16 2 25 1 .C,g '21 3/22iC8 2:00 

# so e 28.50 17 -0 .3 1 5 3 19.7 1.3 063 112 No data 19,4 

## ' .5 0. 94 1C8 38 18.8 2.' 0.83 

### lIS 3 .4 18.2 25 1
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### 5 8iJ9 28.50 18 -0 .3 1 

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# xo oata 19.4 1.5 0,94 "S 3 7 1&8 21 0.83 115 3 .4 18.2 26 1
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### 12 ' 3. '22iCS 245
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### 39 18.2 2.5 10 7 ' 21 3' 22

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## s. 3 19.1 1.3 0 .92 

## u a N o da1a 19.4 1.5 O.9- J 108 38 18.8 2. • 0.86 11 6**3.** 18.2 2 .5 1.06 

### ' 22 3. '22,,03 3:' 5 813 28.5 1 17 · 0,30 5 .6 19.7 1.3 0. 64 

# ,,, No data 19 .4 1.5 0.9 1 

# 10
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## '
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### rs -0 30 

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## o.es 

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# I
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## ns 25 18
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# '"**,~oda ta**  19,4 1.5 0. 90 

### lea 27 18.8 2 .1 0.87 

## trs 22 1 8
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## is

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### o. es 

## ios 30 18.8 2.1 

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### l.C9 123 3i22,,

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### STACK A- 

### inputs STACK B- 

### inputs



## m 775 

## n6 TT1 

# no no 7SO 78 ' 782 763 764 

# 78. 766 787 788 78' 790 791 792 793 

# 7'" 795 7% 797 

# "., m sco 50 ' S02 80J 8C4 805 

### 800 807 

### SO, 800 8 '0 6 " 812 813 614 8" 8 1

S S17 8'8 819 820 

### 82' S22 823 824 825 82S 827 828 

### 829 830 63' 632 28.43 28.43 28.44 28.44 28.44 28
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## 2a."7 2a.48 2a.48 28.48 28.48 28.48 26.49 28.49 28,49 28,49 28,49 28.50 28 .5:) 28
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### 19.7 19.7 

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## 0.'" 0." 0. 93 

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### 0.83 0
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## 0
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### 0.84 0
.... 0.66 0. 8 1 0.80 0. 87 0.97 

### U'4 

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### 1.0< 1. 05 

### '09 ,10 "0 

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# ", 11 ' 1:1 No data NOQala 19,4 No data 19.4 No4lta 19,4 No data 19.4 No data '9.4 Nodata 19.4 NodaJa 19.4 Nodata 19.4 N o data 19.4 Xo data 19.4 Xoo;zb 19.4**~o dala**  19.4 No 6a!a 19.4 Nodala 19.4 Nod ata 19.4 No dala 19.4 No data 19.4 No da!a '9.4 No data 19,4 No datil 19.4 Nodala 19.4 Nod.:lla 19.4 No data 19.4 No data 19.4 No data 19.4 Nodala 19.4 Nodata 19
. 4 No d.lla 19.4 Nodata 19.4 Nodala 19.4 Nodata 19.4 No data 19,4 Nodala 19.4 Nodata 19.4 ,,",od am 19.4 Nodala 19.4 Nodal a 19.4 Noda1.a '9.4 No dala 19
. 4 Noda.ta 19.4 Nodala 19." N()dat3 19
. 4 Nodala 19.4 No data 19,4 

### No data 19,4 No data 19.4 No data 19.4 No data 19.4 No data 19." No data 19.4 Nodnl a 19.4 Nod.:ita 19.4 Noct:l1a 19.4 N()d.lIa 19
. 4 N()da'a 19.4 N()dala 19.4 No dab 19
. 4 N()(jala 19.4



### _ Data no:: va'ld.**~e com** **;x:r:~l** 0( m...atur.-norfll s, ' stem not WOIking. PrCo:ll '.Tl id«ltilied in commen ts. 

### 1
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# '.5 '.5 1.5 1.5 1.5 1.5 1.5 

### 1
.5 1.5

_ , rr. r.:llc wta I.:it!d**IO oO:aj** **:11 4m** **l,lteall6fase ';** **<! oadata** **~tII"** liMJ/l·aI stack ir4>uts 1 0: thaI 15**rr ".t.1epariod** **ust".j** 0 .88 0.86 0.92 0.85 0.85 0.89 0.90 0.90 0.'" 0.65 0.87 0.9 1 0. 9 1 0.88 0
.91 0.93 0.89 0.S5 0.65 0.'" 0.'" 0.a7 0.85 0.86 0
. 65 0. " 0.93 0.68 0. 65 0. 66 0.65 0.85 0.86 0.92 0.9
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... 0. 64 0.90 0
. 88 0.86 0,85 0.e5 0.e6 0.a7 0.87 0.87 0, S7 0.88 0
. 68 0 .65 0.66 Reco: dc.d Data

15- minu(eaverag H



### STACK C· 

### inputs STACK D- 

### inputs**-:- ~~iil'~C)ii;** **j[jI iI:!iii;J~~~PO:** **~A\I9(1 02_Ayg(4)~Vg(4.irfJ0w4j.V:kTmp_F** 

### -Avg(4j 

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### ,ea 

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# ,ea , ea ,os ,C8 

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## e.g F

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. '" 0.61 0.82 0.B3 

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### 0.83 0.88 0.87 0.67 0.86 0.66 0.66 0
. 87 0.96 0 .87 0
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### "6 11. 116 116 116 116 lI S 

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### ' 15 115 2. 1 18.2 2.4 I.OJ 121 2 .0 18.2 2.4 1.04 122 2
. 1 18.2 2.4 1.04 122 2
. 8 18.2 2.4 1.04 121 2
. 9 18.2 2.4 1.05 121 3.0 18.2 2,4 1.06 121 3.0 18.2 2.4 I.CS 122 2.S 18.2 2,4 1 .0.4 122 2.5 18
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### 26 18.2 2.6 1 .07 122 2.4 18.2 2.5 1.03 1 22 2. 4 18.2 2.6 1. 07 123 2.7 18.2 2
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. 9 ,82 la.2 18.2 lS.2 lS.2 18.2 18 ,2 18.2 18.2 lS .2 13 .2 18.2 J 8.2 lB.2 18
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. 5 2.5 2.8 2.. 2. 0 2
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### 2.. 2.5 2.5 

### 2.' 25 2
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# 2.' 2.5 2.5 2 .5 2 .5 

### 1.4 1.1 0


### ' .08 1. 07 

### 1.\0 LCd I.C3 1 .03 

### 1. 09 

### '07 1 .06 '.06 '.08 

### 1.08 1.C9 

### 1.08 I .C? 1. C3 1. 11 I.ca I.Ce I.C9 

### 1.09 1.10 1.1 0 1.10 1.1 0 1.10 

### 1.09 1. 09 1.08 ' 22 '22 

# ", ,2' 

# '2' ,21 ,21 

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### 123 1.22

, 22 '22 ' 22 123

, 22 

### '22
' 22 123 123 '22 123
' 22 

### ,22 

# '2' '22 

### 12' ' 20 Sys lem Bias Dril l Check

# AppendixD Calibration Data 

# AppendixD Calibration Data

# .. BARR S-Type Pitot Tube Geometry Check Inspection Date: 

# Z

# fr j, r Technician: 

# f'tM K7. Function: M-5 Probe 3-1 3ft 

# Pitot Tube Number: 

# _--=-...:-._ Length:



# ---- 1. Are face openings perpendicular to tube axis? 

# Ci YES ( go to 2) 

# o NO (go to 1a) 1a. If NO, is angleless than 10°? 

# o YES( go to 2) 

# D NO (discontinue use) 

# I**r_~~** 

# ------ ------- I J"_ 

### I

# r-~----...: I I 

# 2. Are face openings parallel to longitudinal axis? 

# !Xl YES ( 

# go to 3) 

# D NO (go to 2a) 2a. 

# IfNO, Is angleless than 5·? DYES ( 

# go to 3) 

# D NO (discontinue use) 

# -'Q-**._--~-::** •.-r**----~~-** 

# .f:- w.

# -'~ 

# ......... 

# --

3. Are legs of equal length? 

# I1J YES (go to 4) 

# D NO (go to 3a) 3a. If NO, is differenceless than 1/8 

# inch? 

# o YES ( go to 4) 

# D NO (discontinue use)

# ~----~~~----<=-)---_.

4. 

# Are center-linesof legs coincident? 

# 4a. If NO, are center-lines of face openingsless than 1/32 

# inch? YES ( go to 5) 

# D NO (go to 4a) 

# o YES ( go to 5) 

# o NO (discontinue use)

# --~----r~~----~:7---_· 5. Does this pitot tube passall of the above criteria? 

# tEl YES 

# o NO 

# M,;"",

# S1g"1'!!fJ:--

Revlewed by:

# +..,;~..;:,l{=l!el_~==""j:'-_------ BARR

Pilot Tube Number: _--=-3-...:.1
__ Length:
__ 3_ft

__
1. Are face openings perpendicular to tube axis? 

# Ci YES ( go to 2) 

# o NO (go to 1a) 

# I**r_~~** 

# ------ ------- I J"_ 

### I

# r--~----...: I I


# 2. Are face openings parallel to longitudinal axis? 

# !Xl YES ( 

# go to 3) 

# D NO (go to 2a)

3. Are legs of equal length? 

# I1J YES (go to 4) 

# D NO (go to 3a)

# ~----~~~----<=-)-----

4. 

# Are center-lines of legs coincident?**~** 

# YES ( go to 5) 

# D NO (go to 4a)

# --~----r~~----~~-----
5. Does this pitot tube pass all of the above criteria? 

# S-Type Pitot Tube Geometry Check
Function: 

# M-5 Probe Inspection Date: 

# Z

# fr j, r Technician: 

# f'tM K7..

1a. If NO, is angle less than 10·? 

# o YES ( go to 2)

2a. 

# If NO, Is angle less than 5·? DYES ( 

# go to 3) 

# -'Q-**.---~-::**

1-" 

# D NO (discontinue use)



# D NO (discontinue use)

# ----~~- 

# .f:-
WM

# -'~ 

# ......... 

# --

3a. If NO, is difference less than 1/8 

# inch? 

# o YES ( go to 4) 

# D NO (discontinue use)



# 4a. If NO, are center-lines of face openings less than 1/32 

# inch? 

# o YES ( go to 5) 

# o NO (discontinue use)



# tEl YES 

# o NO

# [-If**~o** 

# tT'fL 

# .. BARR

Pilot Tube Number: 

# '6 - 

# d-- Length: 

# 3'**FUnCtiOn:~** I Free 

# S·Type Pitot Tube Geometry Check 'Inspection Date: Technician:



# -----------

1. Are face openings perpendicular to tube axis?

# ~ES ( goto 2) 

# 0 NO 

# (goto 1a)


# --. I

# 1~~--f--:--X-_:--~------ I l"_ 

### I 

# l- c:.= 

# -;--1
2. ,Are face openings parallelto longitudinalaxis? 

# ""€f YES ( goto 

# 3) 

# 0 NO (go to 2a) ta, 

# If NO, is 

# angleless than 10'? DYES ( go 

# to 2)

# ~, 

# .'**--~-_.**

! !

2a. 

# If NO. is angle Jess than5"""? DYES ( go to 

# 3) 

# o NO (discontinueuse) 

# rL---1!**--~-_.** I I 

# . .

o NO (discontinue use)



# .- -V**~1.** 

# =::=;.;--

. :s:..l._ "..

# ----3~·- 

# . - 

# -

____ _ l:;-



# 3a. If NO. is difference less than 1/8 inch? ... ::

-; 

# 3. Are legs 

# cifequallenglh?, ' 

# " YES ( goto 4)

# '~~~ 

# 0 NO (go to 3a) '.'i.

# --k----~~---~~----- DYES ( go 

# to 4) 

# o NO (discontinue use)

4. Are center-linesof legs coincident?

# ~YES (go 

# to 5) 

# 0 NO (go 

# to 4a)

# --~----~~---=<--)----- 4a. If NO.are center-linesof face openingsless than 1/32 inch? DYES (go to 5) 

# 0 NO (discontinue use)

ReviewedbY:



# -:

.**~'",:** ." 

### . 

# DYES ONO



# BARR

Pitot Tube Number: 

# Length: 

# 3'**FUnCtiOn:~** I Free

1. Are face openings perpendicular to tube axis?

# ~ES ( go to 2) 

# 0 NO 

# (go to 1a)


# --. I

# 1~~--f--:--X--:--~------ I l"_ 

### I

# !-~-;--l
2. ,Are fa:e openings parallel to longitudinal axis? 

# ""€f YES ( go to 3) 

# 0 NO (go to 2a)

...::.". 

# 3. Are legs 

# cifequal length? , ' 

# ,.**~** YES ( go to 4)

# '~~~ 

# 0 NO (go to 3a) -.i.

# --k----~~---~~-----

4. Are center-lines of legs coincident?

# ~YES (go to 5) 

# 0 NO 

# (go to 4a)

# --~----~~---=<--)----.

5. Does this pitot tUDe pass all of the above criteria?

Reviewed by: 

# S- Type Pitot Tube Geometry Check Inspection Date: 

# [-I {**~o** 

# tTech ni cia 

# n: __

# T
__ 'f_L
_____ _

1a, 

# If NO, is 

# angle less than 10'? 

# DYES ( go to 

# 2)

# ~, 

# .'**--~~--.**

! ! 

# o NO (discontinue use) 

# rL.-!!**--~--.** I I 

# , ,

2a. If 

# NO, is angle Jess than 5"""? 

# DYES ( go to 3) 

# o NO 

# (discontinue use)



# .- -V 5 ..**~1.** 

# =::=;.;--

.__ .:s:..l._ "..

# ----3~·- M
_ _



## ____ _ l:;-



# 3a. If NO, is difference less than 1/8 

# inch? 

# DYES ( go to 4) 

# o NO (discontinue use)

4a. If NO, are center-lines of face openings less than 1/32 

# inch? 

# DYES (go to 5) 

# 0 NO (discontinue use)



# DYES ONO

# .. BARR S.Type Pitot Tube Geometry Check



# /-C(-o~ Technician: 

# kIM-I< 'Z... Inspection Date: 

# C-:(

- 

# r Length:



# Funetio~p~~ Free Pltot Tube 

# Number: t-('

1. Are face openings perpendicular to tubeaxis?

**~YES(got02)** 

# 0 NO(got01a) 

# "___ I I



# '~~-f--:-*-_:_-~------- I

_ I



# :----~-l • I 

# 1a. If NO,is angle lessthan10'? DYES (got02) ,

f1..; .-- 

# :1---...-1'

**--~-_.** I I 

# . . o NO (discontinue use)



# --~-~. I I 

# , 

# .
2. Are face openings parallel to longitudinal axis? AYES ( go to 3) 

# o NO(go to 2a) 

# 2a. If NO I 

# is anglelessthan5""'? DYES ( go to 

# 3) 

# o NO (discontinue use)



# ---'-::3~' 

# -

;.. 

# --

____ _ 1::- 

# - 4: _ on r 

# i 

# "',,---='.1./ 

# "1.- .

**~:** 

# "'-

3. Arelegs 

# of equal length? oo..YES( go to 

# 4) 

# o NO (goto 

# 3a) 3a. If NO.is difference lessthan 

# 1/8 Inch? DYES ( goto 4) 

# 0 NO (discontinue use) 

# II/' 

# -\0-----*

**~-:-.** 4a. If NO.are center-lines 

# of face openings less than1/32inch? 4. Are center-lines 

# of legs coincident? pS(YES (go to 5) 

# 0 NO(goto 4a) DYES ( go 

# to 5) 

# o NO (discontinue use)



# --t----~~----<-:)----- 5. Doesthis pilot tubepassall of the above criteria? 

# Techncian



# ~9"! **ujfjj,-+t'i-,~------**

**Re~ewedby. _~~~,_~~~**  _____ 

# ~YES ONO 

# Pito! Tube Number: 

# C-:(

- 

# r Length: t-(f



# Functioesp~~ Free

1. Are face openings perpendicular to tube axis?

**~YES** (go to 

# 2) 

# o NO (go to 1a) 

# I



# '~~-f--:-~--:--~------- I
_ I



# :----~-I I I 

# 2. Are face openings parallel to longitudinal axis? 

# AYES ( go to 3) 

# o NO (go to 2a)



# 3. Are legs of equal length? 

# OO-YES ( go to 

# 4) 

# o NO (go to 3a)

4. Are center-lines of legs coincident? 

# pS(YES (go to 5) 

# 0 NO (go to 4a) 

# --jf----......----'(-:.;;-----

5. Does this pitot tube pass all of tM above criteria? 

# S.Type Pitot Tube Geometry Check Inspection Date:
**/-C(-o~** 

# Technician: 

# kIM-I< 'Z...

1 

# a. If 

# NO, is angle less than 10'? 

# DYES (goI02)

.

f1..; .-- 

# ll---..---/'

**--~--.** I I I • 

# o NO (discontinue use)



# --~-~. I I 

# . .
2a. If NO, is angle less than 5""'? 

# DYES ( go to 3) 

# o NO (discontinue use)



# - 4: _ M ' 

# i 

# "',.---='.1./ "1.-
. ___ **~:** 

# "'-



# ---'-::3~'

# -

;.- 

# -- ____ _ I=-

3a. 

# If NO, is difference less than 

# 1/8 Inch? 

# DYES ( go to 4) 

# 0 NO (discontinue use) 

# II/' 

# -\0-----*

**~-:-.** 4a. If NO, are cenier-lines of face openings less than 1/32 

# inch? 

# DYES ( go to 5) 

# o NO (discontinue use)



# ~YES ONO



# T""ki"~9M! 

# U?fjj
Reviewed by:



# -~+-'f"" **"-'~w;,r,-"-!--=:.L\;,--------**

# Length: 

# .. BARR

PitotTube Number: 

# If' S-TypePitotTube Geometry Check Inspection Date: 

# 11-

# '3 

# t- 0 

# 1- Technlclan: 

# T 

# Y' L

ta, If NO,is anglelessthan 10°? DYES ( go to 2) 

# 1.

**Are.~** 

# openings perpendicular to tube axis?

**~YES(got02)** 

# o NO{got01a) I I I I



# ~~-f--:-~-_:_-~-------

**I-----~-!** f

**~.** I 

# = 

# o NO (discontinueuse) t£y I 

# rL 

# ....!1

**--~-_. --~-_.**  I ! ! !
2. Are face openings parallel to longitudinal axis?



# ~ES(got03) O"NO{got02a) 2a. If NO,is angleless thanS""? DYES ( go 

# to 3) 

# o NO (discontinue use)



# - J- 

# -D 

# -I: 

# *= - h



# --~~ 

# . .,.., "'-.



# 3. Are legs of equal length? 

# lSi' YES ( go to 4) 

# o NO (go to 3a) 3a. If NO,is difference lessthan 

# 1/8 inch? DYES ( go to 4) 

# 0 NO(discontinueuse)



# --t----~~~----~-----
4. Are center-lines of legs coincident?



# ~YES (gotoS) 

# 0 NO (got04a)



# --t----n~----<:3)----- IV



# "-f-----~.-. 4a. If NO,are center-lines offace openingsless than 1/32inch? DYES ( go to 5) 

# 0 NO(discontinueuse)

Reviewed by: 5. Doesthis pitottube passall of the abovecriteria? ...--:-- 

# Technician Signature: 

# S

**C?P~** 

# f1JJ1114k: - l?(YES ONO 

# Pitot Tube Number: Length: 

# If'

1.

**Are.~** 

# openings perpendicular to tube axis?

**~YES(goto2)** 

# o NO{goto1a) 

# I



# ~~-f--:-~--:--~-------

**I---~-!** f

**~.** I 

# 2. Are face openings parallel to longitudinal axis?



# ~ES(goto3) O"NO{got02a)



# 3. Are legs of equal length? 

# lSi' YES ( go to 4) 

# o NO (go 

# 10 3a)



# --t----~~~----~-----
4. Are center-lines of legs coincident?



# ~YES (gotoS) 

# 0 NO (goI04a)



# --t----n~----<:3)-----
5. Does this pitot tube pass all of the above criteria? ...--:-- 

# Technician Signature: 

# S

**~ C?P~**  

# f1iJ1114k: - Reviewed by: 

# S-Type Pitot Tube Geometry Check Inspection Date: 

# 11- 

# '3 

# t- 0 

# fTechnician: 

# T 

# Y' L

1a If 

# NO, is angle less than 10°? DYES ( go to 2) 

# o NO (discontinue l.lSe)



# = t£y • 

# rL 

# ....!1

**--~--. --~--.**  I ! ! !

2a. If NO, is angle less than S..,? DYES ( go 

# to 3) 

# o NO (discontinue use) 

# -D 

# i:

3a. If NO, is difference less than 1/8 

# inch? DYES ( go to 4) 

# 0 NO (discontinue use) 

# IV



# "-f-----~_-.
4a. If NO, are center-lines offace openings less than 1/32 

# inch? DYES ( go to 5) 

# 0 NO (discontinue use)

!?(YES ONO

# THERMOCOUPLE CALIBRATION 

# BARR

Cal Date: 

# THERMOCOUPLE JD TC4-1 1/9/2008 

# M-5 Probe CALIBRATION TECHNICIAN: AGA Hart Scientific 9103-A sin A1B289 Report No. A1B0718 Hart Scientific 9140 sin A1B086 Report No. A1B2024 

# Temperature Calibration Points 32 212 Reference Deg F (To) 32 212 Probe Temp (deg F) 31.1 212 Reference Temp (deg R) deg F + 460 492 672 Probe Temp (deg R), deg F + 460 491.1 672 Difference (degrees) 0.9 0 

# % Diff Abs. T 0.2% 0.0% Is difference less than 1.5% at all measured points? YES REFERENCE STANDARDS TRACEABILITY DATE LABORATORY 12/26/2007 

# Hart Scientific 12/26/2007 

# Hart Scientific 400 650 

# Ambient 400 650 70 399 650 70.5 860 1110 530 859 1110 530.5

1 0 -0.5 0.1% 0.0% 0.1% 

# THERMOCOUPLE CALIBRATION

600 700 800 900 1000 1100 1200 1300 1400 1500 1600 1700 REFERENCE TEMPERATURE, deg.R 

# 500 900 800 

# 700 600 500 400 400 1700 1600 1500 1400 

# " 

# " llf 1300 ::> 

# !;: 

# 1200 0:: 

# 1100 w 

# 1000 ...J 

# a. ::> 

# o o 

# o ::E 0:: W 

# 1=



# Are extrapolated limits less than 1.5%? YES FAHRENHEIT CALIBRATIONRANGE -20 1200 If not acceptable, describe corrective action: Technician signature QA signature 

# THERMOCOUPLE CALIBRATION 

# BARR THERMOCOUPLE JD TC4-1 Cal Date: 1/9/2008 

# M-5 Probe REFERENCE STANDARDS Hart Scientific 9103-A sIn A1B289 Hart Scientific 9140 sIn A1B086 Temperature Calibration Points Reference Deg F (To) Probe Temp (deg F) Reference Temp (deg R) deg F 

# + 460 Probe Temp (deg R), deg F + 460 Difference (degrees) 

# % Diff Abs. T Is difference less than 1.5% at all measured points? TRACEABILITY Report No. A1B0718 Report No. A1B2024 

# 32 212 32 212 31.1 212 492 672 491.1 672

0.9 0 0.2% 0.0% YES CALIBRATION TECHNICIAN: AGA DATE LABORATORY 12126/2007 Hart Scientific 12/26/2007 Hart Scientific 

# 400 650 Ambient 400 650 70 399 650 70.5 860 1110 530 859 1110 530.5

1 0 -0.5 0.1% 0.0% 0.1%

**1700~~~~~~~~~~~~~~~~~~~~~~~~~----~~~~~** 

# 1600~~~~======================~~~~~~~~~~~~~'~~ 

# 1500

**~~"'-"-j**



# ~ 

# 1400

**~~"'-"-j** 

# " 

# ~1300~~~J=~==~=;=======;~=;===;~~~~~~:~~~~~~~~~~ ;;,



# ~ **1200~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~** 0::



# ~ **1100~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~** w

**~ 1000~~~~~~~~~~~--~~~~-~~~~~~~~~~~~--~~~**  ..J Cl. 

# 5 **900~~~~~~~~~~~~~~~--~~~~~~~~~~~~~~~~**



# ~ **800~~~~~~~~~~~~~~~~~~~~~~~~~~~~T.:~~** 0:: 

## w



## ~ **700~~~~~~~~~~~~~~~~~ 600~~~~~~~~~~~~~~~~~**  

## 500~~~~~~~~~~~~~~~~~~~~~~~~~--~--~~~~ **400~~~~~~~~~~~~~~~~~~~~~~~~-'~~~~=T~~** 

# 400 500 600 700 800 900 1000 1100 1200 1300 1400 1500 1600 1700 REFERENCE TEMPERATURE, deg.R 

# Are extrapolated limits less than 1.5%? If not acceptable, describe corrective action: Technician signature QA signature YES FAHRENHEIT CALIBRATION RANGE -20 1200

# THERMOCOUPLE CALIBRATION 

# BARR

Cal Date: 

# THERMOCOUPLE 

# 10 12/31/2007 CALIBRATION TECHNICIAN: 

# TC4·2 M-5 Probe 

# MMK2 Hart Scientific 9103·A 

# sIn A1B289 Report No. A1B0718 Hart Scientific 9140 

# sIn A1B086 Report No. A1B2024 Temperature Calibration Points 32 212 Reference Deg F (To) 31.7 212 Probe Temp (deg F) 31.4 212 Reference Temp (deg R) deg F 

# + 460 491.7 672 Probe Temp (deg R), deg F + 460 491.4 672 Difference (degrees) 0.3 0 % Diff Abs. T 0.1% 0.0% Is difference less than 1.5% at all measured points? YES REFERENCE STANDARDS TRACEABILITY DATE LABORATORY 12/26/2007 Hart Scientific 12/26/2007 Hart Scientific 

# 400 650 Ambient 400 650 69.9 400 650 69.7 860 1110 529.9 860 1110 529.7

0 0 0.2 0.0% 0.0% 0.0% 

# THERMOCOUPLE CALIBRATION 1700 1600 1500 '; 1400 

# " 't:J 

# 1300 :::> 

# 1200

1100 w 

# 1000 oJ Q. 

# is 

# 900 o 

# 800 c:: w 

# i= 

# 700 600 500 400 400 500 600 700 800 900 1000 1100 1200 1300 1400 1500 1600 1700 REFERENCE TEMPERATURE, deg.R 

# Are extrapolated limits less than 1.5%? If not acceptable, describe corrective action: YES FAHRENHEIT CALIBRATION RANGE ·20 1200 Technician signature 

# .1fidIl QA signature 

# Y . .J) \ 

# c.J ........... **ry-~** 

# THERMOCOUPLE CALIBRATION 

# BARR THERMOCOUPLE 10 Cal Date: 

# 12/31/2007 CALIBRATION TECHNICIAN: 

# TC4·2 M-5 Probe 

# MMK2 REFERENCE STANDARDS Hart Scientific 9103·A sIn A1B289 Hart Scientific 9140 sIn A1B086 Temperature Calibration Points Reference Deg F (To) Probe Temp (deg F) Reference Temp (deg R) deg F 

# + 460 Probe Temp (deg R), deg F 

# + 460 Difference (degrees) % Diff Abs. T Is difference less than 1.5% at all measured points? TRACEABILITY Report No. A1B0718 Report No. A1B2024 

# 32 212 31.7 212 31.4 212 491.7 672 491.4 672

0.3 0 0.1% 0.0% YES DATE LABORATORY 

# 12/26/2007 Hart Scientific 

# 12/26/2007 Hart Scientific 

# 400 650 Ambient 400 650 69.9 400 650 69.7 860 1110 529.9 860 1110 529.7

0 0 0.2 0.0% 0.0% 0.0%

**1700.-~~~~~~~~~~~~~~~~~~~~~~~~~~~--~~~~** 

# 1600~~~~====================~~~~~~~~~~~~~~~=~1 

# 1500

**+---~--=J** 

# '; 1400

**+---~--=J** 

# " 

# ~1300~~~~========================~~~~~~c~~~~~~~~i-~~ :::> 

## ~1200~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~ 

# ~1100~~~~~~~~~~~~~~~~~~~~~~~~~~-=~~~~~~ w 

# ~1000~~~~~~~~~~~~~~~~~~~~~~~~~~~~--~~~~~ oJ Q. 

# g **900~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~** ()



# ~ **800~~~~~~~i-i-~~~~~~~~~~=;~~~~~:u~1nrl.~~~** c:: w



## ~ **700~~~~~~~~~~~~~~~~~--~ 600~~~~~~~~~~~~~~~~~~**  

## 500~~~~~~~~~~~~~~-=~~~~~--~~~~--~~~~~~~ **400~~~~~+-~~~~+-~~~--~~~~~+-~~--~+-~~~~+-~~** 

# 400 500 600 700 800 900 1000 1100 1200 1300 1400 1500 1600 1700 REFERENCE TEMPERATURE, deg.R 

# Are extrapolated limits less than 1.5%? YES If not acceptable, describe corrective action: Technician signature 

# .1fid:f

**~** QA signature 

# Y . .J) \

**c.J~ij~** 

# FAHRENHEIT CALIBRATION RANGE ·20 1200

# • BARR THERMOCOUPLE CALIBRATION

Cal Date: 

# THERMOCOUPLE 

# 10 1/9/2008 CALIBRATION TECHNICIAN: 

# TC3-1 M-5 Probe

AGA REFERENCE STANDARDS TRACEABILITY DATE LABORATORY Hart Scientific 9103-A 

# sIn A1B289 Report No. A1B0718 

# 12126/2007 Hart Scientific Hart Scientific 9140 

# sIn A1B086 Report No. A1B2024 

# 12/26/2007 Hart Scientific Temperature Calibration Points 

# 32 212 400 650 Ambient Reference Deg F (To) 32 212 400 650 70 Probe Temp (deg F) 32.8 212 397 634 70.8 Reference Temp (deg R) deg F 

# + 460 492 672 860 1110 530 Probe Temp (deg R), deg F 

# + 460 492.8 672 857 1094 530.8 Difference (degrees) -0.8 0 3 16 -0.8 % Diff Abs. T 0.2% 0.0% 0.3% 1.4% 0.2% Is difference less than 1.5% at all measured points? YES 

# 1700 1600 1500 1400 e 

# " 1300 ::> 

# 1200

1100 w 

# :;; 1000 ..J 

## a. 

# g 900 o 

# 800 0: 

# 700 600 500 400 400 500 600 700 800 900 1000 1100 1200 1300 1400 1500 1600 1700 REFERENCE TEMPERATURE, deg.R Are extrapolated limits less than 1.5%? If not acceptable, describe corrective action: Technician signature QA signature YES FAHRENHEIT CALIBRATION RANGE -20 1200 

# THERMOCOUPLE CALIBRATION 

# BARR THERMOCOUPLE 

# 10 Cal Date: 

# 1/9/2008 CALIBRATION TECHNICIAN: 

# TC3-1 M-5 Probe

AGA REFERENCE STANDARDS Hart Scientific 9103-A 

# sIn A1B289 Hart Scientific 9140 

# sIn A1B086 Temperature Calibration Points Reference Deg F (To) Probe Temp (deg F) Reference Temp (deg R) deg F 

# + 460 Probe Temp (deg R), deg F + 460 Difference (degrees) % Diff Abs. T Is difference less than 1.5% at all measured paints? TRACEABILITY Report No. A1B0718 Report No. A1B2024 

# 32 32 32.8 492 492.8 -0.8 0.2% YES 

# 212 212 212 

# 672 672



# o 0.0% DATE 

# 12126/2007 12/26/2007 

# 400 400 397 860 857

3 0.3% LABORATORY Hart Scientific Hart Scientific 

# 650 Ambient 650 70 634 70.8 1110 530 1094 530.8

16 -0.8 1.4% 0.2%



# 1700 -r-:------------,----,_,,.,.L:L,..-.......,......., 

# 1600~~~r=============================~~~~~~~~~~~~~~~-~·-/~y//>I;

**1500r~~..,**



# .

**~** 

# 1400

**+--'-~~** {l\ 

# ~1300~~~~~~~~~~~~~~~~~~~~~~~~~"~~~~~~~~~~~~ ::>



## ~ **1200~~~~~~~~~~~~~~~~~**

# ____**~~--~~~** 

# ____**~~~~~~**

# ____**~~~~~**



# ~ **1100+-~~~~~~~~~~~~~~~~~~~~~~~-=~~~~~~~~~~~~~** w



# ~ **1000~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~** ..J 

## a. 

# g **900~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~**



# ~ **800~~~~~~~~~~~~~~~~~~~~~~~~m;,~~~:u,~~;T.~~~~~** 0:



# ~ **700~~~~~~~~~~~~~~~~~~~~.., 600~~~~~~~~~~~~~~~~~~~~..,**  **500~~~~~~~~~~~~~~~~~~~~~_".,._".,.~~~-** 

# ____**---------~~~8 400r~~~~~~~~~~~~~~---~~~~--~~~~~~~~~~-~~~~**  

# 400 500 600 700 800 900 1000 1100 1200 1300 1400 1500 1600 1700 REFERENCE TEMPERATURE, deg.R Are extrapolated limits less than 1.5%? YES If not acceptable, describe corrective action: Technician signature QA signature FAHRENHEIT CALIBRATION RANGE -20 1200

# THERMOCOUPLE CALIBRATION 

# BARR

Cal Date: 

# THERMOCOUPLE 10

**TC3~** 

# 1/7/2008 

# M-5 Probe CALIBRATION TECHNICIAN: MMK2 REFERENCE STANDARDS TRACEABILITY DATE LABORATORY Hart Scientific 9103-A 

# sIn A1B289 Report No. A1B0718 

# 12/26/2007 Hart Scientific Hart Scientific 9140 

# sIn A1B086 Report No. A1B2024 

# 12/26/2007 Hart Scientific 

# Temperature Calibration 

# Points 

# 32 212 400 650 

# Ambient Reference Deg F (To) 31.8 212 400 650 70 Probe Temp (deg F) 31.5 211 393 641 69.5 Reference Temp (deg R) deg F + 460 491.8 672 860 1110 530 Probe Temp (deg R), deg F + 460 491.5 671 853 1101 529.5 Difference (degrees) 0.3 1 7 9 0.5 % Diff Abs. T 0.1% 0.1% 0.8% 0.8% 0.1% Is difference less than 1.5% at all measured points? YES 

# THERMOCOUPLE CALIBRATION

600 700 800 900 1000 1100 1200 1300 1400 1500 1600 1700 REFERENCE TEMPERATURE, deg.R 

# 500 900 800 700 600 500 400400 1700 1600 1500 

# i 1400

**~.** 

# 1300 ::> 

# 1200 w 

# 1100 w 

# :;; 1000 .J 0- 

## ::> 

# o o o ::; 0:: 

## w 

## :r 

# ,..

Are extrapolated limits less than 1.5%? YES FAHRENHEIT CALIBRATION RANGE 1500 -20 1200 If not acceptable, describe corrective action: Technician signature QA signature 

# THERMOCOUPLE CALIBRATION 

# BARR THERMOCOUPLE 10 TC3-2 Cal Date: 

# 1/7/2008 

# M-5 Probe CALIBRATION TECHNICIAN: MMK2 REFERENCE STANDARDS TRACEABILITY DATE LABORATORY Hart Scientific 9103-A 

# sIn A 1B289 Report No. A1B0718 

# 12/26/2007 Hart Scientific Hart Scientific 9140 

# sIn A1B086 Report No. A 1B2024 

# 12/26/2007 Hart Scientific 

# Temperature Calibration Points 

# 32 212 400 650 

# Ambient Reference Deg F (To) 31.8 212 400 650 70 Probe Temp (deg F) 31.5 211 393 641 69.5 Reference Temp (deg R) deg F + 460 491.8 672 860 1110 530 Probe Temp (deg R), deg F + 460 491.5 671 853 1101 529.5 Difference (degrees) 0.3 1 7 9 0.5 % Diff Abs. T 0.1% 0.1% 0.8% 0.8% 0.1% Is difference less than 1.5% at all measured points? YES 

# THERMOCOUPLE CALIBRATION **1700r-~~~~~~~~~~------~~--------~~~~--~-------~~~ 1600~~~F-~~~~~~~~~~~'~~~~~~~~~~~~7~~~~**  

# 1500

**-F~'""'-l**



# i1400+=~~.~-=__ 

# ~__ 

# ~ __________

# ~~__ 

# ~~ ..

# ~~~~~~~~~~~~~~~~ **~1300+-~~~~~~~~~~~~~~~~~~~?~~~~~~~~~~~** 

## ::> 

## ~1200+=~~~~~~~~~~~~~~~-=~7~~=-~~--~~~~~~~ w **~1100+-~~~~~~~~~~~~~~~'~~~~~~~~~~~~~~~** 

## w 

# ~1000+=~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~ oJ 0. 

# 5 **900+-~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~** 

# g **800~~~~~~~~~~~~~~~~~~~Thmticm~~Urill~~;rt~~** 0::



# ~ **700+-~~~~~~~~~~~~~~~** 

# ,... 

# 600 **+---'-'--'-'--'-'~~~~--'-'''-''-'--'-'--'-'~--'-'--'-'--'-'--'-'.;.j** 

# --,t::Xt1'apolateCl Calilorat;,nn 

# 500~~~~~~~~~~~~~~==~~~~~~~~~~~ **400+=~~~~~--+-~-r~~~~~~~~~--~~~~~~--~~~~** 

# 400 500 600 700 800 900 1000 1100 1200 1300 1400 1500 1600 1700 REFERENCE TEMPERATURE, deg.R 

# Are extrapolated limits less than 1.5%? If not acceptable, describe corrective action: Technician signature QA signature YES FAHRENHEIT CALIBRATION RANGE 1500 -20 1200

# BARR Engineering Company 

# PYROMETER CALIBRATION**f-~** Pyrometer Number: C \:-\ " 

# G:,.- 

# 1"" 

# c. (f4>iJ..J,'v"'::: {:li( 

# TC,\b) Pyrometer Reference: 

# Gl-**~~** 

# - I

# u..:c')~ -

# ~/Z.**G?,"~il ~c:'39**  

# 0 Date: 

# 3--
. 6 

# gTechnician: 

# p !?",c;Svv/\\CI\-

Reference Pyrometer 

# 1000 

# \.r--tl

# tr950 900 850 800 750 700 650 600 550 

# SOD 450 

# \it 400 350 300 250 200 

# ,.14 150 

# I t)"2. 73 100 j () \ . 

# 0;;- 50 

# 5').7S0 

# l . 0(,.. 

# -50 -L.)}. 

# BARR Engineering Company 

# PYROMETER CALIBRATION**1-~** Pyrometer Number: C \:-\ " 

# G:,.-' 

# c. (f4>iJ..J,'v"'::: {:li( 

# TC,\b) Date: 

# 3--**~** 

# , 6 

# gPyrometer Reference: 

# Gl-**~~** 

# - I

# C;.J.,;C')~ -

# ~/Z. Technician: 

# P!?",C;S\iIr/'\\CI\-**G?<.~il ~c:'39**  

# 0
Reference Pyrometer 

# 1000 

# \.r--t/ " 950 900 850 800 750 700 650 600 550 500 450 

# \it 400 350 300 250 200 '. i.f 

# 150 

# 1')2.73 100 j () \ , 

# 0;;- 50 

# 5').7:;- 0 \. 0(,.. 

# -50 -L.)},**~**

# BARR Engineering Company
Pyrometer Number: 

# c.\4

-5"- 

# r G Pyrometer Reference: 

# ct -**~t- ;(:(.'Cr~-3**  

# iZ 

# lo

# d4 (,,<;. 

# :Yi C' 

# PYROMETER CALIBRATION

Date: 

# .3

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# &,
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# '? Technician: 

# P J(;,sSiA y 1\6 Y

Reference Pyrometer 

# 1000 

# V'--!) (>t950 900 850 800 750 700 650 600 550 500 450 

# ,,' 400 

# '-i 0" • 

# <.. '- 350 

# 350 < 

# '(-z.- 

# 300 

# 6 c 

# L \ <6 250 

# 2. 5 

# r. Y c:, 

# 200 

# (.<)\. 

# of150 

# 152., 

# i-G 100 jU\,

# O~ 50

# 5L1~ 0 {j, 

# (j 

# c;- -50 

# -- Y <& 

# .03 

# BARR Engineering Company
Pyrometer Number:

# C\~ -

# 5"- TG Pyrometer Reference: 

# ct
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# fod4 (,,<;. 

# 3'1"
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# 1000 950 900 850 800 750 700 650 600 550 500 450 400 350 300 250 200 150 100 50 0 -50 

# PYROMETER CALIBRATION

Date: 

# .3

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# &, ,**<..~** 

# '? Technician: 

# P j(;,SSjtV\I1\6Y
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# v-J) (>t-**~'** 

# '-i 0" • 

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# 350 < 

# '('Z.- 

# 6 c 

# '\.,<6 2. 5 \., 

# Y c:,

# C<)\·of152., 

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# O~**5L1~** {j, 

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Pyrometer Number: 

# eJ\, l.\.; 

# c... Pyrometer Reference: Ll 

# -3>-'c\<- -**i~\-** 

# . g j 

# z.. G<:::ji**Co~b1c** 

# PYROMETER CALIBRATION

Date:**~,** 

# (,. 

# coS'" Technician: 

# p. '\4,ssyv'I\\<YY

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# 1000 

# t'-'tll950 900 850 800 750 700 650 600 550 500 450 

# ·31 400 

# yc;" j'? 

# 350 

# !vn·)f 300 

# ',6\. \<'( 250 

# Z. 

# Sl l.)y 

# 200 

# Lui. Ii:.:> 

# 150 

# I 

# S"2... 1(; 100 

# lui.

# 1~ 50 

# 4''2... 

# c \ 0

# I.\~ -50

# Lff.1~ Notes: 

# BARR Engineering Company
Pyrometer Number: 

# eJ\, l\. i 

# c... Pyrometer Reference: Ll 

# -3>!c\<- -**i~\-** 

# .g I 

# z... G<:::li**Co~b1c** 

# Reference 

# 1000 950 900 850 800 750 700 650 600 550 500 450 400 350 300 250 200 150 100 50 0 -50 Notes: 

# PYROMETER CALIBRATION

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# ~

# -S'" Technician: 

# p. ·?e,SSYVI'" \<!IV


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# t'-'Ul-**,~** 

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# q~ 

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# s~l 

# -;a::or. 31 

# t: bO I 

# 1&re 39 ° 

# PYROMETER CALI BRA

# TION

Date: 

# 3 . (.,

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# P.**iS~c;SW"';** I 

# Iw ,
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# 1000 

# f'J 11'>r 950 900 850 800 750 700 650 600 550 500 450**~.;** 

# 400 

# Yol.oi 350 

# 3S'o.d{ 300 

# J 

# ct. l)\a 250 

# (.S"L**L~** 

# 200 

# C. r.::i) 

# ,<7 

# S150 

# ISZ. (. Y 100 

# 1 0 0 

# 9'-i 50 

# 5""1.**CS~** 

# 0 j 

# ('IS 

# -50**'-q~.** 

# 'l.<&
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# BARR Engineering Company
Pyrometer Number:

# q~ 

# - 6--'\<- Pyrometer Reference: Cj - 

# s--x!l -;a::or. 31 '- 

# bOl1 

# &re39C>
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# 1000 950 900 850 800 750 700 650 600 550 500 450 400 350 300 250 200 150 100 50 0 -50 Notes: 

# PYROMETER CALI BRA 

# TION

Date: 

# 3 . (.,

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# <? Technician: 

# P.**iS~c;SW"';** 

# I 

# IeA{' , Pyrometer 

# tJ 11'>r**~1** 

# Yol.oi**3~o.dt** 

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# ,<7 

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# 1 00 

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# C 

# H- l- 

# rc... Pyrometer Reference: C\ - 3>4 - \**t:S.l~f--..s1** 

# t.**~19~03c(** 

# u PYROMETER CALIBRATION

Date: 

# 3 r 

# G ' 

# 06- Technician: 

# e,**KosS\'v\I~I(uY"**

Reference Pyrometer 

# 1000**Ni/~** 

# 950 900 850 800 750 700 650 600 550 500 450 

# \.;, 400 '-1'00, 

# q<Z' 350 

# .s 5""D . () I 

# 300 3CG.**9~** 

# 250 

# '2. 

# S-l. ZS200 '(00·-8<.- 

# 150 

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# 5''(. 51- 100 oc!"- I**,-\~.** <::» 

# 50**~/. &~**  

# 0 O,'j( -50**'-Lj~.** 

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# t.**f.:4'19~<t** 

# 3Cf 

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# 1000 950 900 850 800 750 700 650 600 550 500 450 400 350 300 250 200 150 100 50 0 -50 Notes: 

# PYROMETER CALIBRATION

Date: 

# ::5 r 

# G ' 

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# '-1'00, 

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# k'.oci: 31'"'

# "oI9~" 3';0 

# PYROMETER CALIBRATION

Date: 

# -3. t...., - 

# oC;; Technician: 

# ,p \2--.>5I/V\I' \

# \e.rr·

Reference Pyrometer 

# 1000 

# NIlt950 900 850 800 750 700 650 600 550 500 450 

# "l,j 400 

# yol,_ 

# oS 350 

# 35°, \(., 300 

# '"0 0 ) 

# I**,~** 

# 250 

# Z. )'1, 

# 3'-i 200 

# '( 0/,0; 150 

# I 

# 5"2.. 7-0 100 101, 

# oS 50 

# ?1/.C;L/ 0 

# /, It -50 

# - l-i1, 'be..
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# BARR Engineering Company
Pyrometer Number: (..)1-- \ - 

# Ie Pyrometer Reference: 

# Q -**3~K** - 

# k'.oci= 31'"'**"oI9~"** 3';0 Reference 

# 1000 950 900 850 800 750 700 650 600 550 500 450 400 350 300 250 200 150 100 50 0 -50 Notes: 

# PYROMETER CALIBRATION

Date: 

# .3. t...., - 

# oC;; Technician: 

# .p \2--£5liv\" \

# \e.r(.
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# N//t-

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# oS 350, 1L:. 

# '"0 0 ).

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# "( 0/, 

# oi I 

# 5"2... 7-0 I 01.**o~-** 

# ?J"/.7L/ 

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# I3A.R.R MS ELECTRONIC PRESSURE TRANSDUCER CALIBRATION

MS 1.0. Number: 

# fjS' C Reference 10 No: 

# C'i f. 

# r"' i'-l-00S1) 

# Nlt;,,7/l 1 

# 'l e:

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# ,·W"/:. 7C 6(" 

# 1 Range Setting: (') .- 

# L.. i'

# I~ 1 

# 0 Date of Calibration: 

# .s - c;> - 0 Technician: 

# p, ,'ZvSSyvt:\\erJ' Leak Check: Negative: 

# Ub Positive: 

# A':... @2" @2"
Positive:

Negative:



# Notes:

Barr Engineering Co. 4700 W. 77th St Minneapolis. MN 55437 (952) 832·2600 

# Reference Oil Electric Manometer Pass/Fail Manometer 

# 0.06" l\ 

# fCl-{:S**D·c)~** 

# 0.2" 

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# Pr<S 1" ,**,~** 

# )" 

# .J/r;> 0·
... 

# 1 

# 1.5" r ' 

# L( C(U r r 

# (J:J-) 

# 2" 

# i, 7 4 

# '1 

# Pf.;3 MS ELECTRONIC PRESSURE TRANSDUCER CALIBRATION

MS 1.0. Number: 

# hs, (;, Reference 10 No: 

# C'i f 

# r"' i'-i -00/51 )

# NIt;,,7/!~""'rN"<-7C6(' 

# 1 Range Setting: (\ .- 

# L.. II

# I~ 1 

# 0 Date of Calibration: 

# .s - c::> - 

# 0<6 Technician: 

# ,2· ,'ZvSSyvt:\\er"

Notes:

Barr Engineering Co. 4700 W. 77th St Minneapolis. 

# MN 55437 (952) 832·2600 

# Positive:

Negative: Reference Oil Manometer 

# 0.06" 0.2" 0.5" 0.8"

1" 

# 1.5" 2" Reference Oil

Manometer 

# 0.06" 0.2" 0.5" 0.8"

1" 1.5" 2" Electric Manometer 

# ,I**D'c)~** 

# b. -l 0'1



# O·5'o'r 

# u· '::f'ill 

# i . 00" 

# ....- - 'l /.**~** 

# I I . 

# '7'1 Ii 

# Electric Manometer 

# 6 

# u<- \ "\ U,I/ 

# u- \:,
. qq ,f

"I 

# '?;O{ ( u· .



# ,**,~** 

# )'/ 0·
... 

# 1 r ' L( C(<'I 

# . 7 4 " 

# I , Leak Check: Negative: 

# 4 Positive:**A~** Pass/Fail

# f~s**\J()'SJ;~** 

# 1 

# 1 

# »5**lJr~.s** 

# 'iJD>-S 

# )Jn5 eAh Electric Manometer



# . )?(\-S."5 

# 9[\56 )J{¥:;S 

# yr<s 'Nr;5**~ ~<'** 



# (l:J.) 

# Pf.;3 @2" @2"

# B.A.R.R MS ELECTRONIC PRESSURE TRANSDUCER CALIBRATION

MS I.D. Number: 

# fV\'5," 

# S , . Reference ID No:G':) 

# 1:1

-



# (~. DOS) 

# J l\.Jr 

# S' 

# I



# /IVtejvlc.~ I Range Setting: 

# 0 . (. ;1 

# Hz. a Date of Calibration: 

# 2:>. f..D
. 03' Technician:



# ~<;..s5Vvt 

# ,'l \UV Leak Check: Negative: 

# uk Positive: 

# de. @2" @2" Positive:

Negative:

Notes:

Barr Engineering Co. 4700 W. 77th St Minneapolis, MN 55437 

# (952) 832-2600 

# Reference Oil Electric Manometer Pass/Fail Manometer 

# 0.06" 

# 0, al,"



# l.fI-~ 0.2" 

# 20 II 

# ft>-5.5

**(~')** 

# . 0.5" 

# 0 

# , '-\ 7 If 

# i11>S 0.8" 

# r«, 

# '1-'1 il



# {)('rs.~



# 1" J 

# .0) i\ 

# YtorS-S 1.5" . ".- If 

# \I)p-S -3 I. ') 

# 0 2" 

# 1·1 i I, 

# )J(+C;[;, Reference Oil Electric Manometer Electric Manometer

Manometer 

# 0.06" 

# (), ul/'

**IO~v:;.~** 0.2" 

# " 'L 0/1



# r.~~S '-' 

# - 0.5"

**~,,\I(** 

# \11-(. S 

# O· () 0.8" "- 

## ..... It 

# V(}'sS c) " 

# 7! 1" \) 

# .Cj'j/! 

# . **~[)tSS** 

# 1.5" 

# 4,1



# V('(.~,) f 

# \..,.\ 

# ' 

# 2" 

# I 

# ·1/ " V('0S 

# MS ELECTRONIC PRESSURE TRANSDUCER CALIBRATION

MS I.D. Number: 

# fV\'£,,, 

# S , . Reference ID NO:C':) 

# 1:)

-



# (~. dOS) 

# J l.Jr S' 

# I



# /IVtejvl.c~ I Range Setting: 

# 0 . (. ;1 

# Hz. a Date of Calibration: 

# 2>.

**~** 

# . 0



# ~ Technician: 

# \J£,<i..s5Vv! 

# ,'l\UV

Notes:

Barr Engineering Co. 4700 W. 77th St Minneapolis, MN 55437 

# (952) 832-2600 

# Positive:

Negative: Reference Oil Manometer 

# 0.06" 0.2" 0.5" 0.8"

1" 1.5" 2" Reference Oil

Manometer 

# 0.06" 0.2" 0.5" 0.8"

1" 1.5" 2" Electric Manometer 

# 0, 0(.," 

# 20 1/

**(~)** 

# . 

# o , '-i 

# 7 If



# (\, '1-'1 il 

## '"' ) il 

# J
. 

# u

. ".- If 

# I. ') 

# 0 

# 1·1 i II 

# Electric Manometer 

# LL u(/' " 'LO 'I 

## '-' 

# - t' ,," 

# O· c '" • ,of

**~** 

## It 

# c) " 

# 7'J \).Cj'j/! f 

# 4,1 \.,\ 

# ' 

# I 

# -11 " Leak Check: Negative: G 

# k @ 2" Positive: 

# de. @ 2" Pass/Fail



# l.fI-~ 

# rt'-5.5 

# i11>S ,I)



# ('rs.~ 

# Yt-rS.S \I)p-S .3 )J(+C;[;, Electric Manometer



# IJ~v:;.~

**r.~~S** 

# \11-(. S. y(>-{S

.**~[><SS**



# Vtf.-~.) V('0S

# MS ELECTRONIC PRESSURE TRANSDUCER CALIBRATION

MS I.D. Number:

# ....L{~~S::...-....::;~ 

# __ Reference I DNa: 

# aT I:"T II..i " 0..) '\", 

# N[ S\ /

# ~~"'- 

# J Range Setting: 

# C:::>., 

# 2.- ;'**l~** 

# '2 0 Date of Calibration: 

# 3>' Co
.. 0 ){ 

# Technician: 

# y, i1>S\lY'I·\\c.J'{' Leak Check: Negative: 

# cJkPositive: oj<:.., 

# @2" @2"
Positive:

Negative:



# Notes:

Barr Engineering Co. 4700 W. 77th St Minneapolis, MN 55437 (952) 832-2600 

# Reference Oil Electric Manometer Pass/Fail Manometer 

# 0.06" 

# Oeo "**P~~s.** O· " 

# 0.2" () , "20(1 

# ygS 0.5" 

# o I..j 

# 9 /1

# 1~~f5 0.8" 0·7-"/" 

# ,Jr-. sS

1" 

# ... 7 

# '1/ f 

# -?i\5S 0' 

# 1.5" I., 

# '-I i ,

# i~~ 2" 

# ,g:'**p/~** I ' 

# Reference Oil Electric Manometer Electric Manometer

Manometer 

# 0.06" -L: T,

# }~ 6. v .. 

# 0.2" r, 9!'?:J, 

# n . ''LD 

# 0.5"**().~vf/**

# ~1iS,'; 0.8" 1\ .'6\J;/

# A~5

1" 

# , ()O (I 

# ftrS> I ( 

# 1.5" l ' 

# SD'\ 

# f4):>5 2" 

# ?.
. ..:;:,0 II

# (}~'3$ 

# MS ELECTRONIC PRESSURE TRANSDUCER CALIBRATION

MS I.D. Number:

# ...J.{~~S::....-....::;~

# __ Reference ID No:(hl:"T II...i -

# 0..)·i-I\N[S\/~~"'- 

# J

- Range Setting: 

# C:::>., 

# 2- ;'**l~** 

# '2 0 Date of Calibration: 

# :S. Co
. 0 

# C:{ Technician: 

# Y. i1 ss \lY',·\\c.J'{'

Notes:

Barr Engineering Co. 4700 W. 77th St Minneapolis, MN 55437 (952) 832-2600 

# Positive:

Negative: Reference Oil Manometer 

# 0.06" 0.2" 0.5" 0.8"

1" 1.5" 2" Reference Oil

Manometer 

# 0.06" 0.2" 0.5" 0.8"

1" 1.5" 2" Electric Manometer 0(0 I. 

# O· " ()
. '20(1 

# [) I..J 

# 9" 0·7-"/" 

# " 7'1' f 

# 0' 

# I. 

# '-I**~** i 

## I 

# I ' 

# ,g:' Electric Manometer 

# -L: T. 

# 6. \oJ' 

# o . '"LD r, 

# 0''';V II 

# ()

# .~;I 

# , ()O (I 

# I. 

# /' SD'\ 

# ?.
..:;:,0 II 

# Leak Check: Negative: 

# 2:je:... Positive: 

# oj<:.,
Pass/Fail

# p(l--~s. 

# ygS

# e~f5 

# er.. sS -(1t\5S

# i~~**p/~** Electric Manometer

# }~**9!'?~**

# ~IiSS

# A~5 

# firs> f4):>5**(}~'3$** @2" @2"

# B..A.R.R MS ELECTRONIC PRESSURE TRANSDUCER CALIBRATION

MS 1.0. Number: 

# ;4) 

# S - I , Reference 10 No:

# ~\f.r )<
.._\ 

# -ODS).) 

# NIST

# /f11elv'l:.v\_L;O=f~ ,} Range Setting: 

# Cd**.~** 

# '<, II 

# 11- 1 

# 'J Date of Calibration: 

# 3 -**'::>~** 

# . 

# 0>'.'; Technician:'{), 

# CSSVV)·)\. 

# or - Leak Check: Negative: 

# 4- @ 2" Positive: 

# @ 2"
Positive:

Negative:



# Notes:

Barr Engineering Co. 4700 W. 77th St Minneapolis, MN 55437 (952) 832·2600 

# Reference Oil Electric Manometer Pass/Fail Manometer 

# 0.06" 

# 0, Oe,f7 

# Pry.;,\- 0.2" 

# 0· 

# u::/'**f~** 0.5" _ .. /t

# 17!~~S**u·~u** 

# 0.8" 

# Q. 

# fer i ' 

# H1r:>'S,

1" 

# o 

# 11 '1 

# Pt+C; 

# 1.5" 

# I 1::::/:-(' 

# \..}roC( 

# 2" 

# J. 

# 1'1 II 

# H}%. Reference Oil Electric Manometer Electric Manometer

Manometer 

# 0.06" {I 

# H:rS5 0, 

# o . 0.2" h 

# Z(j' 

# K 1 

# i.' S 

# c· 0.5" 

# 0.5/ 1

• 

# l1tS S 0.8" 

# O. 

# 1-7 I r 

# PI\-:; 

# s

1" / 001'/ 

# p,I}-Ss. 1.5" 

# r J II 

# J::}--li; S 

# 2" 

# 1.15" 

# P'}fS MS ELECTRONIC PRESSURE TRANSDUCER CALIBRATION

MS I.D. Number: 

# ;4) 

# S - I , Reference ID No:

# ~\f.r V"'I-ODSJ.)

# NrST/;11elv'l:.v\'L:O:-f~1 Range Setting: 

# C.d**.~** 

# <. 1/ 

# \1-, '.) Date of Calibration: 

# 3 -**'::>~** 

# . 

# 0'.'; Technician:'{).

# ~ cSSy\! )')\. 

# or -

Notes:

Barr Engineering Co. 4700 W. 77th St Minneapolis, MN 55437 (952) 832-2600 

# Positive:

Negative: Reference Oil Manometer 

# 0.06" 0.2" 0.5" 0.8"

1" 1.5" 2" Reference Oil

Manometer 

# 0.06" 0.2" 0.5" 0.8"



# 1" 1.5" 2" Electric Manometer 

# 0.OC/ 7 

# 0· 

# Wll

_ .. /t

# u·~u 

# Q.I-<);/ U 

# 11 " I 

# c:::r/ f 

# J • 

# ,'1 '/ Electric Manometer**~** {' 

# 0, ()
. h 

# Z(j' 

# c· 0·5/" O. 

# 1-7 I r 

# { 

# 001'/ 

# /.

# ~ J /1 

# 1.15" Leak Check: Negative: 

# 4- @ 2" Positive:

# ~ @ 2" Pass/Fail 

# P.rrs-s,**f~ 17!~~S**  Hlr;>"S, p,q.C;

# )..)~l'S;<: 

# A}%. Electric Manometer 

# H"S5 K1i.'S 

# l1tS S**P.4:;~** J)/'r-SS 

# J-1--li: S 

# P'}-fS

# B.AR.R MS ELECTRONIC PRESSURE TRANSDUCER CALIBRATION

MS 1.0. Number: 

# f1S - 2. , Reference 10 No:

# (A~T 1'-1:,

# oo,r~ Aj;:.r;;T

# )ji~et.'ldyv-.-c~ 1 Range Setting: 

# cJ 

# Z. Hz.O Date of Calibration: 

# .1 r :) - 

# 0 

# g- O D • ( 

# Technician: 

# 't'. )<0.9.5 (V1,) 

# crY: Leak Check: Negative: 

# ok Positive: 

# uk @2" @2"
Positive:

Negative: Reference Oil Electric Manometer Pass/Fail Manometer 

# 0.06" 

# 0,0<0"

# p.~ 0.2" 0, -, 

# 1 (I

# p.~ 

# c. 0.5" 

# 0, 

# S 1 t· 

# V?ffSS 0.8" 

# o . '60'/ 

# 14rss

1" 

# I. 00 1/

# ~1<:£ 1.5" 

# /.47 I'

# /~t£.S. 2" J . 

# 'j 

# 7 ;. Pr}SS. Reference Oil Electric Manometer Electric Manometer

Manometer 

# 0.06" 

# . 7- II 

# e:0-(S 

# (;,0 0.2" 

# 0'2, \ II 

# r 1
, "r$s 

# 0.5" 

# U·50 / 1 

# YrSS 0.8" 

# 0 <:--0 // 

# (1'\-ss, 'c) 

# 1" 

# i, 00 II 

# lJlr( 1.5" I . 

# S-o I{

# p~ 2" 

# "Z ·00 ' J

# \J«-S~ Notes:

Barr Engineering Co. 4700 W. 77th St Minneapolis, MN 55437 (952) 832·2600 

# B.AR.R MS ELECTRONIC PRESSURE TRANSDUCER CALIBRATION

MS 1.0. Number: 

# f1S - 2. , Reference 10 No:

# (A~T /'-1:,

# oo.r~ !\j;:.r;;T

# )ji~et.'lc}V'o-c~ 1 Range Setting: 

# cJ**~** 

# Z. Hz.O Date of Calibration: 

# .1 r :) - 

# 0 

# g- O D I ( 

# Technician: 

# 't'. )<05'.5 (V1,) 

# cry:

Notes:

Barr Engineering Co. 4700 W. 77th St Minneapolis, MN 55437 (952) 832·2600 

# Positive:

Negative: Reference Oil Manometer 

# 0.06" 0.2" 0.5" 0.8"

1" 1.5" 2" Reference Oil

Manometer 

# 0.06" 0.2" 0.5" 0.8"

1" 1.5" 2" Electric Manometer 

# 0,0<.0" O· 

# -z., 1 (I 

# 0, 

# S 1 t·



# . '60'/ (J' 

# I. :'"'\ 1/ 

# uu 

# '·47/' J. 

# 57 it Electric Manometer



# . 7- /1 

# (;.0 

# 0'2, \ II 

# c). 

# )'0 /1 

# o <:--0 r'r .':) 

# i, 00 II 

# I . 

# S-o '{ "Z ·00 ' J 

# Leak Check: Negative: 

# o'k Positive: 

# uk
Pass/Fail 

# Pil-SS**p.~** t?ftSS 

# )4I""SS**~1<:£ l~t£.S.**  Pi''"S.$. Electric Manometer

# ,):~S 

# r 1 ,"rSs 

# YrSS**(~\~** 

# .Pr'r(**p~** \J(
...

# S~ @2" @2"

# B.A.RR MS ELECTRONIC PRESSURE TRANSDUCER CALIBRATION

MS I.D. Number:
...... 

# 1"\...;..2.::..·_'1"--

__ Reference ID No: 

# (Af,l

- 

# H - DOS)) 

# f'Jl- S 

# yf'lbVI'4t i 

# t't -Cu-r 

# I Range Setting: 

# 0 - 1. i'

# I~ 

# z 0 'fjl 

# Date of Calibration: 

# J,. 

# Ii- 0 

# s:; Technician: 

# {J. 

# -b Y"\,' \ 

# \Oy , Leak Check: Negative: 

# de Positive: 

# die @2" @2" Positive:

Negative:

Notes:

Barr Engineering Co. 4700 W. 77th St Minneapolis, MN 

# 55437 (952) 832·2600 

# Reference Oil Electric Manometer Pass/Fail Manometer 

# 0.06" O.oe.;' 

# ?erss 0.2" 

# O·i'1/1 \Jp.-s<;, 

# 0.5" r, 

# Ll 

# '1 fl 

# l?{<-5'S CI. 

# 0.8" D. 

# 1'1 I, 

# ?p..c;.s

1" 

# I. Qo 

# u 

# q .1\- 

# CS 

# 1.5" ').q-:j"

# ~i"r55 2" ! . 

# 77 c: 

# f?'"""s Reference Oil Electric Manometer Electric Manometer

Manometer 

# 0.06" (, 

# Yfl-SS () 

# \.- 

# b . \ 

# c-; \

# 9~,,'S 0.2" 0.5" D- c;()11 

# fl' <;c, 

# 0.8" u·ct;;o 

# ' 

# , (tOj 

# cs.

1" 1. 

# 0 0 'I 

# YC,,"SS 

# 1.5" ! 

# . '_\ <s /I 

# Q.i\-c,t. 

# 2" 

# 1·11 " 

# \/I><S> MS ELECTRONIC PRESSURE TRANSDUCER CALIBRATION

MS I.D. Number:
...... 1"\...;..2.:;..·_· 

# '1"--
__ Reference ID No: 

# (I-\. fl

- 

# H - DOS)) f'J'i-SYf'lbVI'4/t't-CU-r 

# I Range Setting: 

# 0

- 1. i'

# I~ 

# z 0 'fjl 

# Date of Calibration: 

# J,.

# Ii- 0 

# s:; Technician: 

# {J. 

# -\&&s Y"\,' \ 

# \Oy ,

Notes:

Barr Engineering Co. 4700 W. 77th St Minneapolis, MN 

# 55437 (952) 832·2600 

# Positive:

Negative: Reference Oil Manometer 

# 0.06" 0.2" 0.5" 0.8"

1" 1.5" 2" Reference Oil

Manometer 

# 0.06" 0.2" 0.5" 0.8"

1" 1.5" 2" Electric Manometer 

# 0,0(/ 

# O·i'1/1 r, 

# u. 

# Ll 

# '1 fl 

# () , i'1 I,



# /. 00 u 

# '1.L)-=J" ! . 

# 77 t' 

# Electric Manometer (. 

# D_ 1.- 

# b . \ 

# c-; \ 

# D-S(){\ 

# u-ct;)o

# ' 

# , 1. 

# 00 'I 

# ! ._\ 

# <s /I 

# /.11 " Leak Check: Negative: 

# de Positive: 

# die
Pass/Fail 

# ?erss \Jp.-s<;, l?{<-5'S 

# ?{!-c;.s 

# q/\- cs.**~i1'r55** f.",rs Electric Manometer Yfl-SS

# 9~s"S



# f" <;c, 

# (I'r t; 

# s

# yc",ss Q,i\-c,t. 

# \/I><S> @2" @2"

# - BARR ANEROID BAROMETER 

# CALI BRA TION

Barometer I.D. Number: 

# yY'j Zoe 

# 4'7 

# !PrJ3Ii:¥i5 Barometer Reference: 

# 'if,'v'1 C [) 7



# Pretest Calibration: Project Name: 

# yo/\,

# .'1;~1Y1 

# l'Ju '':**(~** 

# ..JV\S; Project Number:

_

Reference ("Hg) Barometer ("Hg) Date Technician Before Adjustment 

# '7_ 

# q,. 36 

# -Z-9. l.<6 "6 .(p**'o"~** 

# ROb After Adjustment 

# Nit- V'J)flr 

# Nfl- IJ\;1...



# Posttest Check: Reference ("Hg) Barometer ("Hg) Date Technician

Notes:

Barr Engineering Co. 4700 W. 77th St Minneapolis, MN 55437 (952) 832·2600 

# ANEROID BAROMETER 

# CALI BRATION

Barometer I.D. Number: yy'j Zoe 

# 4'7

# /PrJ3/~i5 Barometer Reference: 

# 'if,' vI] C [) 7



# Pretest Calibration:
Before Adjustment After Adjustment

Posttest Check:

Notes:

Barr Engineering Co. 4700 W. 77th St Minneapolis, MN 55437 (952) 832-2600 

# Reference ("Hg) 

# 2Q,.36 NA:-

Reference ("Hg) Project Name: 

# yrtA.

# .'1;~11-'l (00 '1

# (~ .. 

# 1V\S; Project Number:
_______ _

Barometer ("Hg) Date Technician



# -25q
. 

# e.g; '6 .(p '0"(; 

# hOb V'J)flr 

# Nfl- IJ\;1...



# Barometer ("Hg) Date Technician

# AppendixE Cylinder Gas Certifications 

# AppendixE Cylinder Gas Certifications

# 3434 Route 22 West, Branchburg, New Jersey 08876 USA ISO 9001:2000

Shipped from: 80 Industrial Drive, Alpha, NJ 08865 

# CERTIFICATE OF ANALYSIS EPA PROTOCOL MIXTURE PROCEDURE # : G1 CUSTOMER: SGI ORDER # : ITEM#: P.O.#: Cherokee Instruments Inc. 0099130 

# 4 8174 

# CYLINDER # : CC-68268 

# CYLINDER PRES: 2000 PSIG 

# CGA OUTLET: 660 

# CERTIFICATION DATE: 11/14/06 

# EXPIRATION DATE: 11/14/2008 CERTIFICATION HISTORY DATE OF MEAN CERTIFIED ANALYTICAL COMPONENT ASSAY CONCENTRATION CONCENTRATION ACCURACY Sulfur Dioxide 11/06/06 48.00 ppm 48.0 ppm +/-1% 11/14/06 47.98 ppm



# BALANCE Nitrogen PREVIOUS CERTIFICATION DATES: None REFERENCE STANDARDS COMPONENT SRM/NTRM# CYLINDER# CONCENTRATION Sulfur Dioxide NTRM-81694 CC-162843 96.1 ppm

INSTRUMENTATION COMPONENT MAKE/MODEL SERIAL # DETECTOR CALIBRATION DATE(S) Sulfur Dioxide Horiba VIA-510 851221093 NDIR 11/14/06

11/14/06 DATE: ..;..;;..

__ ANALYST:

_ THIS STANDARD IS NIST TRACEABLE. IT WAS CERTIFIED ACCORDING TO THE EPA PROTOCOL PROCEDURES. DO NOT USE THIS STANDARD IF THE CYLINDER PRESSURE IS LESS THAN 150 PSIG. 

# //'1 /1 ./

# t~/ 

# --

Tel: +1 908-252-9300 Fax: +1 908-252-0811 www.spectragases.com



# 3434 Route 22 West, Branchburg, New Jersey 08876 USA

Shipped from: 80 Industrial Drive, Alpha, NJ 08865 

# CERTIFICATE OF ANALYSIS
CUSTOMER: SGI ORDER # : Cherokee Instruments Inc. 0099130 ITEM#: 

# 4 P.O.#: 8174 CERTIFICATION DATE: 11/14/06 EXPIRATION DATE: 11/14/2008 CERTIFICATION HISTORY DATE OF MEAN COMPONENT ASSAY CONCENTRATION Sulfur Dioxide 11/06/06 48.00 ppm 11/14/06 47.98 ppm

BALANCE Nitrogen PREVIOUS CERTIFICATION DATES: None REFERENCE STANDARDS COMPONENT SRM/NTRM# CYLINDER# Sulfur Dioxide NTRM-81694 CC-162843

INSTRUMENTATION COMPONENT MAKE/MODEL SERIAL # Sulfur Dioxide Horiba VIA-510 851221093 ISO 9001 :2000



# EPA PROTOCOL MIXTURE PROCEDURE # : G1 CYLINDER # : CC-68268 CYLINDER PRES: 2000 PSIG CGA OUTLET: 660

CERTIFIED ANALYTICAL CONCENTRATION ACCURACY 48.0 ppm +/-1%

CONCENTRATION 96.1 ppm

DETECTOR CALIBRATION DATE(S) NDIR 11/14/06

THIS STANDARD IS NIST TRACEABLE. IT WAS CERTIFIED ACCORDING TO THE EPA PROTOCOL PROCEDURES. DO NOT USE THIS STANDARD IF THE CYLINDER PRESSURE IS LESS THAN 150 PSIG.

# ~ •.)'- //} 

# V j /1 ./

# ~ 

# l/-- ANALYST:
_________ _ DATE:
_____**1_1/_1_4/~06~**

# __ FRED PIKULA
Tel: +1 908-252-9300 Fax: +1 908-252-0811 www.spectragases.com

# Praxair Distribution. Inc 

# 145 Shimersville Road Bethlehem. PA 18015
Tel: 

# (610.1691·2474 Fax: 

# (610l 758-9103 

# CERTIFICATE OF ANALYSIS / EPA PROTOCOL GAS

CUSTOMER P.O NUMBER 1852495-05 

# REFERENCE STANDARD COMPONENT NIST SRi\! NO. CYLINDER NO.**CONCI~NTRA** 

# TION

.**~19** 

### (=,6 FPH 

# ANALYZER READINGS R=REFERENCE ST.4NDARD Z=ZERO GAS 

# C=GAS CMvDlDA.TE

NOt; DISPSRSI\fS INFRAR2D



# 1\'IEAN TEST ASSA)' L8 . S 1 

# l\lEAN TEST ASSAY 1 H _

## J ') 

## HI. 37 

# ts . ].1 

## lS.47 0.2/28iO,/**O_~/16/r.n** 

# CONC. CONe. CONe. 

# C 18.62 

# R 27.20 

# z 0 

# C 1878 

# LAST CALIBRATION DATE SECOND ANALYSIS DATE H27.19 

# C 18.(·8 

# z c R 27 

# 16 

# Z 

# o VIM rPH CONe. 

# :H ." 

# s CONe. 18. 

# ',to 

# CONe. 18. ':.2 

# C ;;i.',;' 

# C :B.6; 

# H 27.% 

## 03/0')/0 7 

# ANALYTICAL PRINCIPLE FIRST ANALYSIS DATE



# Z u 

# R ::"I.OlJ 

# R 2 (j'! 

# Z 

# Z C**l:<l,>'~)**



# CERTIFIED CONCENTRATION TillS CYUNDER NO. :':(:2;885'1 

# liAS BEEN (:ERTIFIED ACCORDING TO SECTION 2.2 

# OF THACEABIUTY PROTOCOL NO. EPA GOO/R9?,' 

## 121 

# PROCEDURE '11 

# CERTIFIED ACCURACY 1 1 

# % 

# NIST TRACEABLE CYLINDER PRESSliHE 200e 

# PSIG CERTIFICATION DATE ,j.l! 

## JO,'T! 

# EXPIRATION**DATI~** 09/16!()'! 

# TERM SULFUR DIOXIDE 

# NITROGEN 18 

## ·HPPI·l Bl\Li'..l'JCE



# ANALYZED BY CERTIFIED BY • / A'') 

# V/

# [l"-) r .,./ -j 

# "--In ; /1 (./ /1, ' 

# r;, ," 

# v ! -'

. 

# Praxair Distribution. hK. 145 Shimt:r,ville Road 

# Bethlehem. Pi\ 18015


# Tel: (610.1691·2474 Fax: (610l 758-9103 

# CERTIFICATE OF ANALYSIS / EPA PROTOCOL GAS

CUSTOMER P.O NUMBER 1852495-05 

# REFERENCE STANDARD CO:\IP01\E;>;T :'I'IST SRi\! ;>;0. 

# CYLINDER :-10. CONCENTRATION

.**~19** 

### (=,6 FPH 

# ANALYZER READINGS R=REFHRENCH ST.4NDARD Z=ZERO 

# GIlS 

# C=GAS C:t{vDlD.4 TF.
A1\AL
......TICAL PRINCIPLE FIRST ANALYSIS DATE



# Z u 

# R :-:"1. O!J 

# R 

# c (j**.~** 

# Z Z**~!** 

# C 1 t-l I,)'} 

## 03,:'0')/('17 

# C ;;, .',:, 

# C :H.6; 

# H n.'J6 

# CONe. ;;' .,," CONe. 18.',,, 

# CONe. :8. ':.2 

# t:/M [,pr·, 

# MEAN TEST ASSAY Lo . S 1



# TillS CYLl1\DER 

# 1'\0. liAS BI£El\ CERTIFIED ACCORDING TO SECTIOl\ 2.2 

# OF TRACEABII.ITY PROTOCOL l\0. PROCEDURE ';1 

# CERTIFIED ACCURACY 1 1 

# % 

# NIST TRACEABLE CYLINDER PRESSliRE ;:00,' 

# 1'51(; CERTIFICATIOJ', DATE 'J.!! 

## 16!T! 

# F:XPIRATIO:-;**DATI~** 

# TER:'tJ



# ANALYZED BY 

# z [,' 

# R 27 

# Z [}

## U/~I 

# .16 

# LAST CALIBRATION DATE 

# SECOND ANALYSIS DATE H27.19 

# C 18,(·8 

# Z I) 

# C 18.78 

# C 1S. 02 

# R 27.20 

# CONC. lB
. .\7 

# CONe. Ill. 

## J 1 

# CONe. lH.4·; [';:':-1 

# rvlEAN TEST ASSAY 1 it.

## ~ 

## 9



# CERTIFIED CONCENTRATION 18 

## ·HPPI·! 

# NlTROGEN Bl\Li\NCE



# CERTIFIED BY • / A'') 

# V/ [,
...,) 

# r .,./

# elill SCOTT-MARRIN, INC. 6531 BOX SPRINGS BLVD. • RIVERSIDE, CA 92507 TELEPHONE (95t) 653·6780 • FAX (95t ) 653 - 2430 

# Report Of Analysis EPA Protocol Gas Mixtures BARR01 TO: 

# Barr Engineering Co Attn: Pete Rossmiller 4700 

# West 77th Street Minneapolis, MN 55435-4803 (952) 832-2890 REPORT NO: 

# 50895-02 REPORT DATE: 

# November 30, 20060 CUSTOMER PO NO: 

# 20060926TL

CYLINDER NUMBER: 

# CC106732 CYLIN DER SIZE: 150A (1,,1,1 std cu 

# ft) CYLlNDER PRESSURE: 2000 psig

COMPONENT CONCENTRATION 

# (v/v) REFERENCE ANALYZER EXPIRATION REPLICATE 

# ± EPA UNCERTAINTY STANDARD MAKE,MODEL, 

## SIN,DETECTION 

# DATE ANALYSIS DATA Carbon dioxide 8.98 ±O.09 % GMIS Varian Model 1860 

# 11/28/2009 11/28/2006 CYLINDER#: Serial # None 8.98 % CC42814 Thermal Conductivity 8.99 % @8% Gas Chromatography 8.98 % LAST CAL DATE: 

# 1112812006 MEAN: 

# 8.98 % Oxygen 8.95 

# ± 0.05 % GMIS Varian Model 1860 11130/2009 11/3012006 CYLlNDER#: Serial 

# # None 8.95% CC81204 Thermal Conductivity 8.95 % @9.88% Gas Chromatography 8.96 % LAST CAL DATE: 

# 11/9/2006 MEAN: 

# 8.95 % Nitrogen Balance

ppm 

# = umole/mole 

# % 

# = mole-% 

# The above analyses were performedin accordancewith ProcedureG1 of the EPA Traceability Protocol, ReportNumber EPA·600/R97/121, dated September 1997. The above analyses are inva Id if 

# the ylinder pressureis less than 150psig.


# ANALYST: APPROVED: 

# M.S.Calhoun 

# jJ.T.Marrin The only liabilityof this companyfor gas whichfails to complywith thisanalysisshall be replacementor reanalysisthereof by the companywithoutextracost. 

# STANDARD CALIBRATION GASES IN ALUMINUM CYLINDERS 

# elill SCOTT-MARRIN, INC. 6531 BOX SPRINGS BLVD. • RIVERSIDE, CA 92507 TELEPHONE (95 t) 653·6780 • FAX (95 t ) 653·2430 

# Report Of Analysis EPA Protocol Gas Mixtures BARR01 REPORT NO: 

# 50895.02 TO: 

# Barr Engineering Co Attn: Pete Rossmiller 4700 

# West 77th Street Minneapolis, MN 55435-4803 (952) 832-2890 REPORT DATE: 

# November 30, 20060 CUSTOMER PO NO: 

# 20060926TL

CYLINDER NUMBER: 

# CC106732 CYLIN DER SIZE: 150A (1,,1,1 std Cl! 

# ft) CYLlNDER PRESSURE: 2000 psig

COMPONENT CONCENTRATION 

# (v/v) REFERENCE ANALYZER EXPIRATION REPLICATE 

# ± EPA UNCERTAINTY STANDARD MAKE, MODEL. 

## SIN, DETECTION 

# DATE ANALYSIS DATA Carbon dioxide B.98 ±O.09 % GM1S Varian Model 1860 

# 11/28/2009 11/28/2006 CYLINDER#: Serial # None 8.98 % CC42814 Thermal Conductivity 8.99 % @8% Gas Chromatography 8.98 % LAST CAL DATE: 

# 11/28/2006 MEAN: 

# 8.98 % Oxygen 8.95 

# ± 0.05 % GMIS Varian Model 1860 

# 11/30/2009 11/30/2006 CYLINDER#: Serial 

# # None 8.95% CC81204 Thermal Conductivity 8.95 % @9.88% Gas Chromatography 8.96 % LAST CAL DATE: 

# 11/9/2006 MEAN: 

# 8.95 % Nitrogen Balance

ppm 

# = umole/mole 

# % 

# = mole-% 

# The above analyses were perfonned in accordance 

# with Procedure G1 of the EPA Traceability Protocol, Report Number EPA·600/R971121, dated September 1997. The above analyses are in va 'd if the ylinder pressure is less than 150 psig.


# ANALYST: APPROVED: 

# ~ M.S.Calhoun 

# jJ.T.Marrin
The only liaoility of this company for gas which fails to comply with this analysis shall be replacement or reanalysis thereof by the company without extra cost. 

# STANDARD CALIBRATION GASES IN ALUMINUM CYLINDERS

# 51111 SCOTT-MARRIN, INC. 6531 BOX SPRINGS BLVD. II 

# RIVERSIDE, CA 92507 TELEPHONE (951) 653- 6780 II 

# FAX (951) 653- 2430 

# Report Of 

# Analysis EPA Protocol Gas Mixtures BARR01 TO: 

# Barr Engineering Co Attn: Pete Rossmiller 7390 OHMS Lane Edina, MN 55439-2330 (952) 832-2890 REPORT NO: 

# 52716-03 REPORT DATE: 

# November 6,20070 CUSTOMER PO NO: 

# 2007/09/20TYL 

# 1

CYLINDER NUMBER: 

# CC62111 CYLINDER SIZE.:t50A.(141l>tdcu ft). 

# .CVLlNDERPRESSURE:2000 psig

COMPONENT CONCENTRATION (vlv) REFERENCE ANALYZER EXPIRATION 

# ± EPA UNCERTAINTY STANDARD MAKE, MODEl., SIN, DETECTION 

# DATE REPLICATE ANALYSIS DATA Carbon dioxide

Oxygen 

# 5.05 ±0.05 %



# 21.00 ± 

# 0.22 % GMIS 

# CYLINDER#: CC83094 

# @8.1 % GMIS 

# CYLINDER 

# #: AlM031591 @24.4% Varian Model 

# 1860 11/5/2010 Serial 

# # None Thermal Conductivity Gas Chromatography LAST CAL DATE: 

# 11/5/2007 MEAN: 

# Varian Model 

# 1860 11/2/2010 Serial 

# # None Thermal Conductivity Gas Chromatography LAST CAL DATE: 

# 10/26/2007 MEAN: 

# 11/512007 

# 5.05% 5.05% 5.05% 5.05% 11/2/2007 

# 21.01 

# % 21.01 % 

# 20.99 % 21.00 

# % Nitrogen Balance

ppm 

# =umole/mole 

# % 

# = mole-% The above analyses were performed in accordance with Procedure G1 of the EPA Traceability Protocol, Report Number EPA·600/R97/121, dated September 1997. The above analyses are inva id if the ylinder pressure is less than 150 psig.


# ANALYST:

# --->"--:::;;'~bC-"'-=-"""";:;;--'---- APPROVED: 

# ---r..:-------- M.S.Calhoun 

# L J. T. Marrin The only liabilityof this company for gas which falls to comply with this analysis shall 

# be replace ent or reanalysis thereof by the company without extra cost. 

# STANDARD CALIBRATION GASES IN ALUMINUM CYLINDERS 

# 51111 SCOTT-MARRIN, INC. 6531 BOX SPRINGS BLVD. II 

# RIVERSIDE, CA 92507 TELEPHONE (951) 653- 6780 II 

# FAX (951) 653- 2430 

# Report Of 

# Analysis EPA Protocol Gas Mixtures BARR01 REPORT NO: 

# 52716-03 TO: 

# Barr Engineering Co 

# Attn: Pete Rossmiller 7390 OHMS Lane Edina, MN 

# 55439-2330 (952) 832-2890 REPORT DATE: 

# November 6,20070 CUSTOMER PO NO: 

# 2007/09/20TYL 1

CYLINDER NUMBER: 

# CC62111 CYL!NDER SIZE.: .1.50A.(141l>tdcu ft). 

# .CVLlNDERPRESSURE:2000 psig

COMPONENT CONCENTRATION 

# (vlv) REFERENCE ANALYZER EXPIRATION REPLICATE 

# ± EPA UNCERTAINTY STANDARD MAKE, MODEL, SIN, DETECTION 

# DATE ANALYSIS DATA Carbon dioxide 5.05 ±0.05 % GMIS Varian Model 1860 

# 11/5/2010 11/5/2007 CYLINDER#: Serial 

# # None 5.05% CC83094 Thennal Conductivity 5.05% @8.1 % Gas Chromatography 5.05% LAST CAL DATE: 

# 11/5/2007 MEAN: 

# 5.05% Oxygen 21.00 ± 0.22 % GMIS Varian Model 

# 1860 11/2/2010 11/2/2007 CYLINDER#:: Serial 

# # None 21.01 % AlM031591 Thennal Conductivity 21.01 % @24.4% Gas Chromatography 20.99 

# % LAST CAL DATE: 

# 10/26/2007 MEAN: 

# 21.00 % Nitrogen Balance

ppm 

# = umolelmole 

# % 

# = mole-% The above analyses were performed in accordance with Procedure G1 of the EPA Traceability Protocol, Report Number EPA-600/R97/121, dated September 1997. The above analyses are inva id if the ylinder pressure is less than 150 psig.


# ANALYST:
____

# -4~~~~~~_______ 

# APPROVED:
____

# ~~~----'------------ M.S.Calhoun 

# L J. T. Marrin The only liability of this company for gas which fails 

# to comply with this analysis shall be replace en! 

# or reanalysIs thereof 

# by the company 

# w,thout extra cost. STANDARD CALIBRATION GASES IN ALUMINUM CYLINDERS

# AppendixF Process Operating Data 

# AppendixF Process Operating Data

# ArcelorMittal Mincora Mine Pellet Plant Process Rates During 802 Testing


# GP2 GFR5 P1 GP2-GFR5 timestamp A104CV07CNVYR_A106CV05CNVYR_A11 OCV02CNVYR_SCALE_LSTHR_ V, 

# 3/10/2008 0:00 340 90 227 250 3/10/2008 1:00 342 89 224 253 3/10/2008 2:00 343 93 226 250 3/10/2008 3:00 340 90 225 250 3/10/20084:00 342 105 222 237 3/10/2008 5:00 338 116 202 222 3/10/20086:00 346 100 213 246 3/10/20087:00 347 90 231 256 3/10/20088:00 339 86 231 253 3/10/20089:00 205 54 159 151 3/10/200810:00 302 90 210 212 3/10/2008 11:00 344 88 188 255 3/10/2008 12:00 350 111 211 239 3/10/2008 13:00 355 112 213 243 3/10/200814:00 361 102 226 259 3/10/2008 15:00 360 98 235 262 3/10/2008 16:00 360 95 240 264 3/10/2008 17:00 362 102 234 260 3/10/2008 18:00 362 103 234 259 3/10/2008 19:00 362 103 234 259 3/10/200820:00 361 98 233 263 3/10/2008 21:00 360 98 236 262 3/10/2008 22:00 353 92 233 260 3/10/200823:00 363 101 239 262

3/11/20080:00 355 95 233 261 3/11/2008 1:00 347 89 235 258 3/1112008 2:00 346 86 235 259 3/11/20083:00 343 86 230 257 3/11/20084:00 342 83 236 258 3/11/20085:00 336 84 232 252 3/11/20086:00 343 88 229 255 3/11/20087:00 346 94 234 252 3/11/2008 8:00 348 93 225 255 3/11/2008 9:00 339 97 228 242 3/11/2008 10:00 342 108 220 234 3/11/2008 11:00 332 109 199 223 3/11/200812:00 314 104 198 210 3/11/2008 13:00 304 96 177 208 3/11/200814:00 302 86 151 216 3/11/200815:00 312 89 197 224 3/11/200816:00 310 93 201 217 3/11/200817:00 314 93 207 221 3/11/200818:00 334 102 197 231 3/11/2008 19:00 348 105 222 243 3/11/200820:00 353 99 220 254 3/11/200821 :00 360 99 229 261 3/11/200822:00 231 252

3/12/20080:00 3/12/2008 1:00 3/12/2008 2:00 3/12/20083:00 3/12/20084:00 3/12/20085:00 3/12/2008 6:00 3/12/20087:00 3/12/2008 8:00 3/12/2008 9:00 3/12/2008 10:00 3/12/2008 11:00 3/12/200812:00 3/12/200813:00 349 348 348 347 352 357 353 344 358 357 362 358 356 351 98 104 109 92 97 106 107 108 117 113 101 99 94 94 Page 1 of6 228 223 218 220 231 228 225 218

328 251 243 239 255 254 250 245 237 241 244 262 260 263 257 

# ArcelorMittal Mincora Mine Process Rates During S02 Testing Pellet Plant GP2 GFR5 

# P1 GP2-GFR5 timestamp A 104CV07CNVYR_ A 106CV05CNVYR_ A 11 OCV02CNVYR_SCALE_LSTHR_ V, 

# 3/10/2008 0:00 

# 340 90 227 250 3/10/2008 

# 1:00 342 89 224 253 3/10/2008 2:00 

# 343 93 226 250 3/10/2008 3:00 

# 340 90 225 250 3/10/20084:00 

# 342 105 222 237 3/10/20085:00 

# 338 116 202 222 3/10/2008 6:00 

# 346 100 213 246 3/10/20087:00 

# 347 90 231 256 3/10/20088:00 

# 339 86 231 253 3/10/2008 9:00 

# 205 54 159 151 3/10/2008 

# 10:00 302 90 210 212 3/10/2008 

# 11 :00 344 88 188 255 3/10/2008 12:00 

# 350 111 211 239 3/10/200813:00 

# 355 112 213 243 3/10/200814:00 

# 361 102 226 259 3/10/2008 15:00 

# 360 98 235 262 3/10/2008 16:00 

# 360 95 240 264 3/10/2008 17:00 

# 362 102 234 260 3/10/2008 18:00 

# 362 103 234 259 3/10/2008 19:00 

# 362 103 234 259 3/10/200820:00 

# 361 98 233 263 3/10/2008 

# 21 :00 360 98 236 262 3/10/2008 22:00 

# 353 92 233 260 3/10/200823:00 

# 363 101 239 262

3/11/20080:00 

# 355 95 233 261 3/11/2008 

# 1:00 347 89 235 258 3/11/20082:00 

# 346 86 235 259 3/11/20083:00 

# 343 86 230 257 3/11/20084:00 

# 342 83 236 258 3/11/20085:00 

# 336 84 232 252 3/11/20086:00 

# 343 88 229 255 3/11/20087:00 

# 346 94 234 252 3/11/2008 8:00 

# 348 93 225 255 3/11/2008 9:00 

# 339 97 228 242 3/11/2008 

# 10:00 342 108 220 234 3/11/2008 

# 11 :00 332 109 199 223 3/11/2008 12:00 

# 314 104 198 210 3/11/2008 13:00 

# 304 96 177 208 3/11/2008 14:00 

# 302 86 151 216 3/11/2008 15:00 

# 312 89 197 224 3/11/200816:00 

# 310 93 3/11/2008 17:00 

# 314 93 3/11/2008 18:00 

# 334 102 3/11/2008 19:00 

# 348 105 3/11/200820:00 

# 353 99 3/11/200821 :00 

# 360 99 3/11/200822:00

3/12/20080:00 

# 349 98 251 3/12/2008 

# 1:00 348 104 243 3/12/2008 2:00 

# 348 109 239 3/12/20083:00 

# 347 92 255 3/12/20084:00 

# 352 97 254 3/12/20085:00 

# 357 106 250 3/12/2008 6:00 

# 353 107 245 3/12/20087:00 

# 344 108 237 3/12/2008 8:00 

# 358 117 241 3/12/2008 9:00 

# 357 113 244 3/12/2008 

# 10:00 362 101 262 3/12/2008 

# 11: 00 358 99 260 3/12/200812:00 

# 356 94 263 3/12/200813:00 

# 351 94 328 257 Page 1 of6

# ArcelorMittal Mincora Mine Pellet Plant Process Rates During 802 Testing
GP2 GFR5 P1 GP2-GFR5 timestamp A104CV07CNVYR_ A106CV05CNVYR_A11OCV02CNVYR_SCALE_LSTHR_V, 

# 3/12/200814:00 3/12/2008 15:00 3/12/200816:00 3/12/2008 17:00 3/12/2008 18:00 3/12/2008 19:00 3/12/200820:00 3/12/200821:00 3/12/200822:00 3/12/2008 23:00

3/13/2008 0:00 3/13/2008 1 

# :00 3/13/2008 2:00 3/13/2008 3:00 3/13/20084:00 3/13/2008 5:00 3/13/2008 6:00 3/13/20087:00 3/13/2008 8:00 3/13/2008 9:00 3/13/2008 

# 10:00 3/13/2008 11 

# :00 3/13/2008 12:00 3/13/2008 13:00 3/13/200814:00 3/13/2008 15:00 3/13/2008 16:00 3/13/2008 17:00 3/13/2008 18:00 3/13/2008 19:00 3/13/2008 20:00 3/13/200821 :00 3/13/2008 22:00 3/13/2008 23:00

3/14/20080:00 3/14/2008 

# 1:00 3/14/20082:00 3/14/20083:00 3/14/20084:00 3/14/20085:00 3/14/20086:00 3/14/20087:00 3/14/20088:00 3/14/20089:00 3/14/200810:00 3/14/2008 11 

# :00 3/14/200812:00 3/14/200813:00 3/14/2008 14:00 3/14/2008 15:00 3/14/2008 16:00 3/14/2008 17:00 3/14/200818:00 3/14/2008 19:00 3/14/200820:00 3/14/200821 :00 3/14/200822:00 3/14/2008 23:00

3/15/2008 0:00 3/15/2008 1 

# :00 3/15/2008 2:00 3/15/2008 3:00 

# 344 348 358 340 346 351 354 343 342 341 339 337 341 332 333 331 314 325 335 333 337 339 340 352 346 358 359 352 354 359 354 353 351 345 350 354 356 345 342 343 339 333 333 346 341 339 342 347 355 349 357 351 353 353 347 93 93 98 95 93 95 98 101 99 105 103 92 93 89 88 92 92 91 87 94 93 91 87 94 92 95 100 95 91 97 103 91 90 93 99 91 93 89 88 88 91 88 88 104 106 102 102 95 104 98 102 102 110 110 100

Page 2 of6 346 225 364 318 214 230 222 226 209 216 205 215 218 215 219 215 205 192 218 217 213 216 223 234 225 226 229 231 233 229 231 222 239 224 227 229 232 231 230 224 228 222 222 219 219 201 218 213 227 220 223 221 217 217 223 251 255 260 245 253 256 256 243 243 237 236 245 248 243 245 239 223 234 248 239 244 248 254 259 254 262 259 257 263 262 251 262 261 252 251 263 263 256 254 255 249 245 245 243 235 237 239 252 251 250 255 249 243 243 247 ArcelorMittal Mincora Mine Process Rates During 802 Testing Pellet Plant GP2 GFR5 P1 GP2-GFR5 timestamp A 1 04CV07CNVYR_ A 106CV05CNVYR_ A 11 OCV02CNVYR_SCALE_LSTHR_ 

# V, 

# 3/12/200814:00 

# 344 93 346 251 3/12/2008 15:00 

# 348 93 225 255 3/12/200816:00 

# 358 98 364 260 3/12/2008 17:00 

# 340 95 318 245 3/12/2008 18:00 

# 346 93 214 253 3/12/2008 19:00 

# 351 95 230 256 3/12/200820:00 

# 354 98 222 256 3/12/200821:00 

# 343 101 226 243 3/12/200822:00 

# 342 99 209 243 3/12/2008 23:00 

# 341 105 216 237

3/13/2008 0:00 

# 339 103 205 236 3/13/2008 

# 1:00 337 92 215 245 3/13/2008 2:00 

# 341 93 218 248 3/13/2008 3:00 

# 332 89 215 243 3/13/20084:00 

# 333 88 219 245 3/13/2008 5:00 

# 331 92 215 239 3/13/2008 6:00 

# 314 92 205 223 3/13/20087:00 

# 325 91 192 234 3/13/2008 8:00 

# 335 87 218 248 3/13/2008 9:00 

# 333 94 217 239 3/13/2008 

# 10:00 337 93 213 244 3/13/2008 

# 11 :00 339 91 216 248 3/13/2008 12:00 

# 340 87 223 254 3/13/2008 13:00 

# 352 94 234 259 3/13/200814:00 

# 346 92 225 254 3/13/2008 15:00 

# 358 95 226 262 3/13/2008 16:00 

# 359 100 229 259 3/13/2008 17:00 

# 352 95 231 257 3/13/2008 18:00 

# 354 91 233 263 3/13/2008 19:00 

# 359 97 229 262 3/13/2008 20:00 

# 354 103 231 251 3/13/200821 :00 

# 353 91 222 262 3/13/2008 22:00 

# 351 90 239 261 3/13/2008 23:00 

# 345 93 224 252

3/14/20080:00 

# 350 99 227 251 3/14/2008 

# 1:00 354 91 229 263 3/14/20082:00 

# 356 93 232 263 3/14/20083:00 

# 345 89 231 256 3/14/20084:00 

# 342 88 230 254 3/14/20085:00 

# 343 88 224 255 3/14/20086:00 

# 339 91 228 249 3/14/20087:00 

# 333 88 222 245 3/14/20088:00 

# 333 88 222 245 3/14/20089:00 

# 346 104 219 243 3/14/200810:00 

# 341 106 219 235 3/14/2008 

# 11 :00 339 102 201 237 3/14/200812:00 

# 342 102 218 239 3/14/200813:00 

# 347 95 213 252 3/14/2008 14:00 

# 355 104 227 251 3/14/2008 15:00 

# 349 98 220 250 3/14/2008 16:00 

# 357 102 223 255 3/14/2008 17:00 

# 351 102 221 249 3/14/200818:00 

# 353 110 217 243 3/14/2008 19:00 

# 353 110 217 243 3/14/200820:00 

# 347 100 223 247 3/14/200821 :00 3/14/200822:00 3/14/2008 23:00

3/15/2008 0:00 3/15/2008 

# 1:00 3/15/2008 2:00 3/15/2008 3:00 

# Page 2 of6

# ArcelorMittal Mincora Mine Pellet Plant Process Rates During 802 Testing
GP2 GFR5 P1 GP2-GFR5 timestamp A104CV07CNVYR_ A106CV05CNVYR_A11OCV02CNVYR_SCALE_LSTHR_Vi 

# 3/15/2008 4:00 3/15/2008 5:00 3/15/20086:00 3/15/2008 7:00 3/15/2008 8:00 3/15/2008 9:00 3/15/2008 

# 10:00 3/15/2008 

# 11:00 3/15/200812:00 3/15/2008 13:00 3/15/200814:00 3/15/2008 15:00 3/15/2008 16:00 3/15/200817:00 3/15/2008 18:00 3/15/2008 19:00 3/15/2008 20:00 3/15/200821 :00 3/15/2008 22:00 3/15/2008 23:00

3/16/2008 0:00 3/16/2008 

# 1:00 3/16/2008 2:00 3/16/2008 3:00 3/16/2008 4:00 3/16/20085:00 3/16/20086:00 3/16/20087:00 3/16/2008 8:00 3/16/2008 9:00 3/16/2008 

# 10:00 3/16/2008 

# 11:00 3/16/2008 12:00 3/16/2008 13:00 3/16/200814:00 3/16/200815:00 3/16/200816:00 3/16/2008 17:00 3/16/2008 18:00 3/16/2008 19:00 3/16/2008 20:00 3/16/2008 

# 21:00 3/16/2008 22:00 3/16/2008 23:00

3/17/20080:00 3/17/20081:00 3/17/20082:00 3/17/20083:00 3/17/20084:00 3/17/20085:00 3/17/20086:00 3/17/20087:00 3/17/20088:00 3/17/20089:00 3/17/200810:00 3/17/200811:00 3/17/200812:00 3/17/2008 13:00 3/17/200814:00 3/17/200815:00 

# 340 100 240 3/17/200816:00 

# 347 96 252 3/17/200817:00 

# 350 94 256 Page 3 of6 ArcelorMittal Mincora Mine Pellet Plant Process Rates During S02 Testing
GP2 GFR5 P1 GP2-GFR5 timestamp A 104CV07CNVYR_ A 1 06CV05CNVYR_ A 11 OCV02CNVYR_SCALE_LSTHR_ Vi 

# 3/15/2008 4:00 3/15/2008 5:00 3/15/20086:00 3/15/2008 7:00 3/15/2008 8:00 3/15/2008 9:00 3/15/2008 

# 10:00 3/15/2008 

# 11 :00 3/15/200812:00 3/15/2008 13:00 3/15/200814:00 3/15/2008 15:00 3/15/2008 16:00 3/15/200817:00 3/15/2008 18:00 3/15/2008 19:00 3/15/2008 20:00 3/15/200821 :00 3/15/2008 22:00 3/15/2008 23:00

3/16/2008 0:00 3/16/2008 

# 1 :00 3/16/2008 2:00 3/16/2008 3:00 3/16/2008 4:00 3/16/20085:00 3/16/20086:00 3/16/20087:00 3/16/2008 8:00 3/16/2008 9:00 3/16/2008 

# 10:00 3/16/2008 

# 11 :00 3/16/2008 12:00 3/16/2008 13:00 3/16/200814:00 3/16/200815:00 3/16/200816:00 3/16/2008 17:00 3/16/2008 18:00 3/16/2008 19:00 3/16/2008 20:00 3/16/2008 

# 21 :00 3/16/2008 22:00 3/16/2008 23:00

3/17/20080:00 3/17/20081:00 3/17/20082:00 3/17/20083:00 3/17/20084:00 3/17/20085:00 3/17/20086:00 3/17/20087:00 3/17/20088:00 3/17/20089:00 3/17/200810:00 3/17/200811:00 3/17/200812:00 3/17/2008 13:00 3/17/200814:00 3/17/200815:00 

# 340 100 240 3/17/200816:00 

# 347 96 252 3/17/200817:00 

# 350 94 256 Page 3 of6

# ArcelorMittal Mincora Mine Pellet Plant Process Rates During S02 Testing


# GP2 GFR5 P1 GP2·GFR5 timestamp A104CV07CNVYR_A106CV05CNVYR_A11 OCV02CNVYR_SCALE_LSTHR_ VI 

# 3/17/200818:00 354 101 254 3/17/200819:00 354 93 262 3/17/200820:00 359 97 262 3/17/200821:00 349 88 260 3/17/200822:00 356 91 265 3/17/200823:00 354 95 239 259

3/18/20080:00 348 92 291 256 3/18/2008 1:00 344 89 367 256 3/18/2008 2:00 344 86 309 258 3/18/2008 3:00 341 82 230 259 3/18/20084:00 332 77 349 255 3/18/2008 5:00 336 80 228 256 3/18/20086:00 331 80 329 251 3/18/20087:00 329 79 225 250 3/18/2008 8:00 327 80 219 247 3/18/2008 9:00 332 89 220 243 3/18/200810:00 331 86 218 245 3/18/2008 11:00 332 83 232 249 3/18/200812:00 332 81 299 251 3/18/2008 13:00 336 86 222 249 3/18/2008 14:00 329 80 225 248 3/18/200815:00 331 80 224 251 3/18/200816:00 329 81 225 248 3/18/2008 17:00 335 93 221 242 3/18/2008 18:00 334 109 215 225 3/18/2008 19:00 334 107 197 227 3/18/2008 20:00 329 105 200 223 3/18/200821:00 331 105 199 226 3/18/2008 22:00 332 93 204 239 3/18/200823:00 334 90 218 244

3/19/2008 0:00 328 90 282 239 3/19/2008 1:00 346 91 307 254 3/19/2008 2:00 349 94 270 255 3/19/2008 3:00 346 91 240 255 3/19/20084:00 345 96 227 249 3/19/2008 5:00 341 88 223 253 3/19/20086:00 346 94 224 252 3/19/2008 7:00 347 90 229 257 3/19/20088:00 345 88 231 257 3/19/2008 9:00 345 88 305 257 3/19/2008 10:00 344 88 230 257 3/19/2008 11:00 346 90 234 256 3/19/2008 12:00 346 86 327 261 3/19/2008 13:00 349 86 243 263 3/19/200814:00 339 83 227 256 3/19/2008 15:00 344 88 233 256 3/19/200816:00 344 85 230 259 3/19/2008 17:00 343 83 320 260 3/19/2008 18:00 345 87 234 258 3/19/2008 19:00 330 85 252 245 3/19/2008 20:00 331 87 286 244 3/19/200821:00 331 89 224 243 3/19/200822:00 338 90 216 248 3/19/200823:00 334 89 221 245

3/20/20080:00 341 89 279 252 3/20/2008 1:00 348 89 294 260 3/20/2008 2:00 347 93 255 254 3/20/2008 3:00 350 94 318 256 3/20/2008 4:00 343 91 294 252 3/20/2008 5:00 343 97 265 246 3/20/2008 6:00 345 92 252 252 3/20/2008 7:00 348 90 235 259 Page 4 of6 

# ArcelorMittal Mincora Mine Process Rates During S02 Testing Pellet Plant GP2 GFR5 P1 GP2·GFR5 timestamp A 104CV07CNVYR_ A 1 06CV05CNVYR_ A 11 OCV02CNVYR_SCALE_LSTHR_ VI 

# 3/17/2008 18:00 

# 354 101 254 3/17/200819:00 

# 354 93 262 3/17/200820:00 

# 359 97 262 3/17/200821:00 

# 349 88 260 3/17/200822:00 

# 356 91 265 3/17/200823:00 

# 354 95 239 259

3/18/2008 0:00 

# 348 92 291 256 3/18/2008 

# 1:00 344 89 367 256 3/18/2008 2:00 

# 344 86 309 258 3/18/2008 3:00 

# 341 82 230 259 3/18/20084:00 

# 332 77 

# 349 255 3/18/2008 5:00 

# 336 80 228 256 3/18/2008 6:00 

# 331 80 329 251 3/18/20087:00 

# 329 79 225 250 3/18/2008 8:00 

# 327 80 219 247 3/18/2008 9:00 

# 332 89 220 243 3/18/2008 

# 10:00 331 86 218 245 3/18/2008 

# 11 :00 332 83 232 249 3/18/2008 12:00 

# 332 81 299 251 3/18/2008 13:00 

# 336 86 222 249 3/18/2008 14:00 

# 329 80 225 248 3/18/2008 15:00 

# 331 80 224 251 3/18/200816:00 

# 329 81 225 248 3/18/200817:00 

# 335 93 221 242 3/18/2008 18:00 

# 334 109 215 225 3/18/2008 19:00 

# 334 107 197 227 3/18/2008 20:00 

# 329 105 200 223 3/18/2008 

# 21 :00 331 105 199 226 3/18/2008 22:00 

# 332 93 204 239 3/18/2008 23:00 

# 334 90 218 244

3/19/2008 0:00 

# 328 90 282 239 3/19/2008 

# 1:00 346 91 307 254 3/19/2008 2:00 

# 349 94 270 255 3/19/2008 3:00 

# 346 91 240 255 3/19/20084:00 

# 345 96 227 249 3/19/2008 5:00 

# 341 88 223 253 3/19/20086:00 

# 346 94 224 252 3/19/2008 7:00 

# 347 90 229 257 3/19/2008 8:00 

# 345 88 231 257 3/19/2008 9:00 

# 345 88 305 257 3/19/2008 

# 10:00 344 88 230 257 3/19/2008 

# 11 :00 346 90 234 256 3/19/2008 12:00 

# 346 86 327 261 3/19/2008 13:00 

# 349 86 243 263 3/19/200814:00 

# 339 83 227 256 3/19/2008 15:00 

# 344 88 233 256 3/19/200816:00 

# 344 85 230 259 3/19/2008 17:00 

# 343 83 320 260 3/19/2008 18:00 

# 345 87 234 258 3/19/2008 19:00 

# 330 85 252 245 3/19/2008 20:00 

# 331 87 286 244 3/19/2008 

# 21 :00 331 89 224 243 3/19/2008 22:00 

# 338 90 216 248 3/19/2008 23:00 

# 334 89 221 245

3/20/2008 0:00 

# 341 89 279 252 3/20/2008 

# 1:00 348 89 294 260 3/20/2008 2:00 

# 347 93 255 254 3/20/2008 3:00 

# 350 94 318 256 3/20/2008 4:00 

# 343 91 294 252 3/20/2008 5:00 

# 343 97 265 246 3/20/2008 6:00 

# 345 92 252 252 3/20/2008 7:00 

# 348 90 235 259 Page 4 of6

# ArcelorMittal Mincora Mine Pellet Plant Process Rates During 802 Testing


# GP2 GFR5 P1 GP2-GFR5 timestamp A104CV07CNVYR_ A106CV05CNVYR_A11OCV02CNVYR_SCALE_LSTHR_VI 

# 3/20/20088:00 342 88 231 253 3/20/2008 9:00 343 90 225 253 3/20/2008 10:00 340 85 222 254 3/20/2008 11:00 350 95 227 255 3/20/2008 12:00 338 97 222 241 3/20/2008 13:00 345 100 235 245 3/20/200814:00 338 101 287 237 3/20/2008 15:00 354 113 230 241 3/20/2008 16:00 343 108 236 235 3/20/2008 17:00 348 113 225 235 3/20/2008 18:00 344 107 213 237 3/20/2008 19:00 345 111 209 234 3/20/2008 20:00 340 97 211 243 3/20/200821:00 335 95 220 240 3/20/2008 22:00 338 99 209 239 3/20/200823:00 351 99 218 252

3/21/20080:00 345 93 228 252 3/21/20081:00 343 96 219 247 3/21/20082:00 338 93 220 246 3/21/20083:00 339 93 232 247 3/21/20084:00 340 92 275 248 3/21/20085:00 341 91 235 250 3/21/20086:00 337 98 219 239 3/21/20087:00 339 93 217 246 3/21/20088:00 341 89 222 252 3/21/20089:00 335 84 226 251 3/21/200810:00 343 85 224 258 3/21/2008 11:00 343 82 233 261 3/21/200812:00 341 82 235 259 3/21/200813:00 344 85 225 259 3/21/200814:00 343 89 229 254 3/21/200815:00 344 86 234 258 3/21/200816:00 341 87 238 254 3/21/200817:00 349 85 281 264 3/21/200818:00 345 87 227 258 3/21/200819:00 330 82 308 248 3/21/200820:00 335 82 278 253 3/21/200821:00 332 82 240 250 3/21/200822:00 332 81 222 251 3/21/200823:00 337 84 229 254

3/22/2008 0:00 336 83 226 254 3/22/2008 1:00 332 84 229 248 3/22/20082:00 328 81 223 247 3/22/20083:00 338 87 217 251 3/22/20084:00 345 88 234 257 3/22/2008 5:00 348 91 228 257 3/22/2008 6:00 346 89 228 257 3/22/2008 7:00 341 92 233 250 3/22/20089:00 335 92 216 243 3/22/2008 10:00 333 96 222 237 3/22/2008 11:00 334 99 203 236 3/22/2008 12:00 328 81 219 247 3/22/2008 13:00 334 88 220 247 3/22/2008 14:00 347 93 221 254 3/22/2008 15:00 347 100 227 246 3/22/2008 16:00 353 98 222 256 3/22/2008 17:00 351 105 228 246 3/22/2008 18:00 351 107 227 244 3/22/2008 19:00 277 93 322 183 3/22/2008 20:00 346 101 177 244 Page 5 of6 

# ArcelorMittal Mincora Mine Process Rates During S02 Testing Pellet Plant GP2 GFR5 Pi GP2-GFR5 timestamp A 104CV07CNVYR_ A 106CV05CNVYR_ A 11 OCV02CNVYR_SCALE_LSTHR_ VI 

# 3/20/2008 8:00 

# 342 88 231 253 3/20/2008 9:00 

# 343 90 225 253 3/20/2008 

# 10:00 340 85 222 254 3/20/2008 

# 11 :00 350 95 227 255 3/20/2008 12:00 

# 338 97 222 241 3/20/2008 13:00 

# 345 100 235 245 3/20/200814:00 

# 338 101 287 237 3/20/2008 15:00 

# 354 113 230 241 3/20/2008 16:00 

# 343 108 236 235 3/20/2008 17:00 

# 348 113 225 235 3/20/2008 18:00 

# 344 107 213 237 3/20/2008 19:00 

# 345 111 209 234 3/20/2008 20:00 

# 340 97 211 243 3/20/200821 :00 

# 335 95 220 240 3/20/2008 22:00 

# 338 99 209 239 3/20/2008 23:00 

# 351 99 218 252

3/21/20080:00 

# 345 93 228 252 3/21/2008 

# 1:00 343 96 219 247 3/21/20082:00 

# 338 93 220 246 3/21/20083:00 

# 339 93 232 247 3/21/20084:00 

# 340 92 275 248 3/21/2008 5:00 

# 341 91 235 250 3/21/20086:00 

# 337 98 219 239 3/21/20087:00 

# 339 93 217 246 3/21/20088:00 

# 341 89 222 252 3/21/20089:00 

# 335 84 226 251 3/21/2008 

# 10:00 343 85 224 258 3/21/2008 

# 11 :00 343 82 233 261 3/21/200812:00 

# 341 82 235 259 3/21/2008 13:00 

# 344 85 225 259 3/21/200814:00 

# 343 89 229 254 3/21/2008 15:00 

# 344 86 234 258 3/21/200816:00 

# 341 87 238 254 3/21/200817:00 

# 349 85 281 264 3/21/200818:00 

# 345 87 227 258 3/21/200819:00 

# 330 82 308 248 3/21/200820:00 

# 335 82 278 253 3/21/200821 :00 

# 332 82 240 250 3/21/200822:00 

# 332 81 222 251 3/21/200823:00 

# 337 84 229 254

3/22/2008 0:00 

# 336 83 226 254 3/22/2008 

# 1:00 332 84 229 248 3/22/2008 2:00 

# 328 81 223 247 3/22/2008 3:00 

# 338 87 217 251 3/22/20084:00 

# 345 88 234 257 3/22/2008 5:00 

# 348 91 228 257 3/22/2008 6:00 

# 346 89 228 257 3/22/2008 7:00 

# 341 92 233 250 3/22/20089:00 

# 335 92 216 243 3/22/2008 

# 10:00 333 96 222 237 3/22/2008 

# 11 :00 334 99 203 236 3/22/2008 12:00 

# 328 81 219 247 3/22/2008 13:00 

# 334 88 220 247 3/22/2008 14:00 

# 347 93 221 254 3/22/2008 15:00 

# 347 100 227 246 3/22/2008 16:00 

# 353 98 222 256 3/22/2008 17:00 

# 351 105 228 246 3/22/2008 18:00 

# 351 107 227 244 3/22/2008 19:00 

# 277 93 322 183 3/22/2008 20:00 

# 346 101 177 244 Page 5 of6

# ArcelorMittal Mincora Mine Pellet Plant Process Rates During 802 Testing


# GP2 GFR5 P1 GP2-GFR5 timestamp A104CV07CNVYR_ A106CV05CNVYR_A11OCV02CNVYR_SCALE_LSTHR_ VI 

# 3/22/2008 21:00 349 109 214 239 

# 3/22/2008 22:00 348 95 225 253 

# 3/22/2008 23:00 360 98 227 262



# 3/23/2008 0:00 349 88 232 261 

# 3/23/2008 1:00 357 100 234 257 

# 3/23/2008 2:00 346 103 223 243 

# 3/23/2008 3:00 336 94 209 242 

# 3/23/20084:00 341 95 297 245 

# 3/23/2008 5:00 347 94 236 253 

# 3/23/2008 6:00 353 96 226 258 

# 3/23/2008 7:00 354 115 226 239 

# 3/23/2008 8:00 354 118 210 237 

# 3/23/20089:00 346 106 213 241 

# 3/23/200810:00 345 108 219 238 

# 3/23/2008 11:00 344 123 205 220 

# 3/23/2008 12:00 334 97 198 237 

# 3/23/2008 13:00 337 87 222 249 

# 3/23/200814:00 356 95 225 261 

# 3/23/200815:00 354 109 231 245 

# 3/23/2008 16:00 352 108 291 244 

# 3/23/2008 17:00 342 116 341 226 

# 3/23/2008 18:00 350 110 211 240 

# 3/23/2008 19:00 348 92 291 256 

# 3/23/2008 20:00 349 94 255 255 

# 3/23/2008 21:00 335 84 228 251 

# 3/23/2008 22:00 342 88 228 255 

# 3/23/2008 23:00 346 88 224 257



# 3/24/2008 0:00 346 94 235 252 

# 3/24/2008 1:00 344 92 229 253 

# 3/24/2008 2:00 339 90 221 249 

# 3/24/2008 3:00 345 88 302 257 

# 3/24/20084:00 360 96 347 264 

# 3/24/2008 5:00 349 91 240 257 

# 3/24/2008 6:00 349 93 305 256 

# 3/24/20087:00 352 90 229 261 

# 3/24/20088:00 349 89 315 260 

# 3/24/2008 9:00 356 91 341 266 

# 3/24/2008 10:00 353 88 278 265 

# 3/24/2008 11:00 360 95 325 264 

# 3/24/200812:00 355 102 247 253 

# 3/24/2008 13:00 350 108 224 243 

# 3/24/2008 14:00 347 95 218 252 

# 3/24/2008 15:00 357 100 230 257 

# 3/24/2008 16:00 353 96 232 257 

# 3/24/200817:00 356 87 237 269 

# 3/24/200818:00 347 91 230 255 

# 3/24/200819:00 352 97 227 254 

# 3/24/200820:00 361 111 226 251 

# 3/24/2008 21:00 353 117 228 236 

# 3/24/200822:00 348 104 212 243 

# 3/24/2008 23:00 349 93 221 256



# 3/25/2008 0:00 349 91 232 257 

# 3/25/2008 1:00 352 100 227 252 

# 3/25/2008 2:00 354 102 225 251 

# 3/25/20083:00 347 97 222 250 

# 3/25/20084:00 347 96 222 251 

# 3/25/2008 5:00 346 96 225 250 

# 3/25/2008 6:00 348 98 224 250 

# 3/25/2008 7:00 340 92 223 248 

# 3/25/20088:00 351 103 224 247 

# 3/25/20089:00 342 93 219 249
Page 6 of6 

# ArcelorMittal Mincora Mine Process Rates During S02 Testing Pellet Plant GP2 GFR5 P1 GP2-GFR5 timestamp A 104CV07CNVYR_ A 106CV05CNVYR_ A 11 OCV02CNVYR_SCALE_LSTHR_ VI 

# 3/22/2008 

# 21 :00 349 109 214 239 3/22/2008 22:00 

# 348 95 225 253 3/22/2008 23:00 

# 360 98 227 262

3/23/2008 0:00 

# 349 88 232 261 3/23/2008 

# 1:00 357 100 234 257 3/23/2008 2:00 

# 346 103 223 243 3/23/2008 3:00 

# 336 94 209 242 3/23/20084:00 

# 341 95 297 245 3/23/2008 5:00 

# 347 94 236 253 3/23/2008 6:00 

# 353 96 226 258 3/23/2008 7:00 

# 354 115 226 239 3/23/2008 8:00 

# 354 118 210 237 3/23/2008 9:00 

# 346 106 213 241 3/23/2008 

# 10:00 345 108 219 238 3/23/2008 

# 11 :00 344 123 205 220 3/23/2008 12:00 

# 334 97 198 237 3/23/2008 13:00 

# 337 87 222 249 3/23/200814:00 

# 356 95 225 261 3/23/200815:00 

# 354 109 231 245 3/23/2008 16:00 

# 352 108 291 244 3/23/2008 17:00 

# 342 116 341 226 3/23/2008 18:00 

# 350 110 211 240 3/23/2008 19:00 

# 348 92 291 256 3/23/2008 20:00 

# 349 94 255 255 3/23/2008 

# 21 :00 335 84 228 251 3/23/2008 22:00 

# 342 88 228 255 3/23/2008 23:00 

# 346 88 224 257

3/24/2008 0:00 

# 346 94 235 252 3/24/2008 

# 1:00 344 92 229 253 3/24/2008 2:00 

# 339 90 221 249 3/24/2008 3:00 

# 345 88 302 257 3/24/20084:00 

# 360 96 347 264 3/24/2008 5:00 

# 349 91 240 257 3/24/2008 6:00 

# 349 93 305 256 3/24/20087:00 

# 352 90 229 261 3/24/2008 8:00 

# 349 89 315 260 3/24/2008 9:00 

# 356 91 341 266 3/24/2008 

# 10:00 353 88 278 265 3/24/2008 

# 11 :00 360 95 325 264 3/24/2008 12:00 

# 355 102 247 253 3/24/2008 13:00 

# 350 108 224 243 3/24/2008 14:00 

# 347 95 218 252 3/24/2008 15:00 

# 357 100 230 257 3/24/2008 16:00 

# 353 96 232 257 3/24/200817:00 

# 356 87 237 269 3/24/2008 18:00 

# 347 91 230 255 3/24/200819:00 

# 352 97 227 254 3/24/2008 20:00 

# 361 111 226 251 3/24/2008 

# 21 :00 353 117 228 236 3/24/2008 22:00 

# 348 104 212 243 3/24/2008 23:00 

# 349 93 221 256

3/25/2008 0:00 

# 349 91 232 257 3/25/2008 

# 1:00 352 100 227 252 3/25/2008 2:00 

# 354 102 225 251 3/25/2008 3:00 

# 347 97 222 250 3/25/20084:00 

# 347 96 222 251 3/25/2008 5:00 

# 346 96 225 250 3/25/2008 6:00 

# 348 98 224 250 3/25/2008 7:00 

# 340 92 223 248 3/25/2008 8:00 

# 351 103 224 247 3/25/2008 9:00 

# 342 93 219 249
Page 6 of6

# Appendix G Stack Test Plan 

# Appendix G Stack Test Plan

# Test Plan For Temporary SOx Monitoring Installation at a Taconite Manufacturing Facility
Date Test Plan created/revised: February 8, 2008 Scheduled Test Dates: March 11-18, 2008


# PART I: General Information Emissions facility location Facility contact Testing company contact ArcelorMittal Minorca Mine, Jaime Baggenstoss Richard Berg Inc. Environmental Engineer Sr. Air Quality Technician 5950 Old Highway 53 ArcelorMittal Minorca Mine, Inc. Barr Engineering Company P.O. Box 1 P.O. Box 1 4700 West 77th 

# Street Virginia, MN 55792 Virginia, MN 55792 Minneapolis, MN 55431 

# Minnesota Air Emissions Permit Number: 13700062-002 (issued February 12,2007) 

# AQD File Number: 257 

# Reason emissions units are to be tested: Arcelor-Mittal Mincora Mine (Mittal) will undertake testing to provide additional sulfur dioxide emissions (S02) data for evaluation of the proposed BART S02 limits. S02 concentration data will be collected simultaneously from the four induration furnace stacks of Emissions Unit EU026. Data will be collected at variable process conditions for up to 150 hours. The table below provides the emissions units' plant nomenclature, permit identification and plant location. Stack drawings showing stack dimensions and test port orientation and locations relative to airflow disturbances are attached.

Process unit Emissions unit Stack vent Emissions unit location nomenclature number number Stacks A-D EU026 SV014, SV015, Bldg 007 Pellet Plant indurating furnace SV016, SV017 stacks


# PART II: Testing Requirements The following table identifies pollutants to be determined; applicable emissions limit and units, and associated rezulation for each emissions unit and stack vent '0' 

# Process unit Stack Pollutant Specific Methods/Procedures Required nomenclature vent Tested/Permit Citation number Limit Indurating furnace SV014, S02 Testing is voluntary and will be conducted in waste gas stacks SV015, concentration general accordance with Minn. Rules and US A, B,C, 

# 0 SV016, and mass EPA test methods. SV017 emissions rates 

# Test Plan For Temporary SOx Monitoring Installation at a Taconite Manufacturing Facility
Date Test Plan created/revised: February 8, 2008 Scheduled Test Dates: March 11-18, 2008


# PART I: General Information Emissions facility location Facility contact ArcelorMittal Minorca Mine, Jaime Baggenstoss Inc. Environmental Engineer 5950 Old Highway 53 ArcelorMittal Minorca Mine, Inc. P.O. Box 1 P.O. Box 1 Virginia, MN 55792 Virginia, MN 55792 Testing company contact Richard Berg Sr. Air Quality Technician Barr Engineering Company 4700 West 77th 

# Street Minneapolis, MN 55431 

# Minnesota Air Emissions Permit Number: 13700062-002 (issued February 12,2007) 

# AQD File Number: 257 

# Reason emissions units are to be tested: Arcelor-Mittal Mincora Mine (Mittal) will undertake testing to provide additional sulfur dioxide emissions (S02) data for evaluation of the proposed BART S02 limits. S02 concentration data will be collected simultaneously from the four induration furnace stacks of Emissions Unit EU026. Data will be collected at variable process conditions for up to 150 hours. The table below provides the emissions units' plant nomenclature, permit identification and plant location. Stack drawings showing stack dimensions and test port orientation and locations relative to airflow disturbances are attached.

Process unit Emissions unit Stack vent Emissions unit location nomenclature number number Stacks A-D EU026 SV014, SV015, Bldg 007 Pellet Plant indurating furnace SV016, SV017 stacks


# PART II: Testing Requirements The following table identifies pollutants to be determined; applicable emissions limit and units, and associated reaulation for each emissions unit and stack vent '0' 

# Process unit Stack Pollutant Specific Methods/Procedures Required nomenclature vent Tested/Permit Citation number Limit Indurating furnace SV014, S02 Testing is voluntary and will be conducted in waste gas stacks SV015, concentration general accordance with Minn. Rules and US A, B,C, 

# 0 SV016, and mass EPA test methods. SV017 emissions rates

# EPA test method modifications are detailed In 

# Section VI. 2 

# A 50-day period for submission of the final report is requested as noted in Section VI Test Report.



# Process unit Stack Pollutant Specific Methods/Procedures Required nomenclature vent Tested/Permit Citation number Limit Permit limit for Testing performed by : S02: 40 CFR Part 60, appendix A There is no SOx concentration by modified EPA Method S02 emissions 6C 1 

# limit when firing Volumetric airflow rate by modified EPA on natural gas Method 2 1 

# Gas analysis for determination of dry molecular weight by modified EPA Method 3A 1 

# Moisture content by modified EPA Method 4 1 1



# Part ill: 

# Operating Conditions Mittal intends to vary process operations within the target ranges listed in the table below during the testing program. Process Parameters to be Monitored Process Parameter Units Frequency Range Pellet type 

# -- -- 100% Flux 

# Ferrous iron content of percent 24-hr 61-63 estimated 

# feed material (filter cake) composite 

# Green feed to grate LTPH 1 

# Shift tonnage 

# Production rate (finished LTPH 1 

# Shift tonnage 310-370 

# pellet) Heat 

# input" A 

# = last firing chamber MCF/h 3 

# Hourly average A: 

# TBD B 

# =first firing chamber B:TBD C 

# = preheat burners C:TBD A -130,000-165,000 

# Stack gas flow rate dscfm 4 

# B -126,000-156,000 continuous monitoring of gas Hourly average C -105,000-164,000 flow rate (test company) D-128,000-162,000 

# Combustion zone degrees F Hourly average TBD 

# temperature Fuel type 

# -- 

# -- Natural Gas 

# Unusual production events 

# -- As needed 

# -- Ambient temperature degrees F Hourly average 

# -- 1 

# LTPH (Long tons per hour) are an average for the 8-hour shift 2 

# Limited history on A 

# & B lower burners 3 

# MCF/hr (standard cubic feet of gas burned per hour), at 1000 Btu/scf 4 

# dscfm (dry standard cubic feet per minute) Flow rate is not readily adjustable


# 2

Process unit Stack Pollutant Specific Methods/Procedures Required nomenclature vent Tested/Permit Citation number Limit Permit limit for Testing performed by : S02: 40 CFR Part 60, appendix A There is no SOx concentration by modified EPA Method S02 emissions 6C 1 limit when firing Volumetric airflow rate by modified EPA on natural gas Method 21 Gas analysis for determination of dry molecular weight by modified EPA Method 3A 1 Moisture content by modified EPA Method 4 1 1 

# EPA test method modifications are detailed In 

# Section VI. 2 

# A 60-day period for submission of the final report is requested as noted in Section VI Test Report. 

# Part ill: 

# Operating Conditions Mittal intends to vary process operations within the target ranges listed in the table below during the testing program. Process Parameters to be Monitored Process Parameter Units Frequency Pellet type 

# -- -- Ferrous iron content of percent 24-hr 

# feed material (filter cake) composite 

# Green feed to grate LTPH 1 Shift tonnage 

# Production rate (finished LTPH 1 Shift tonnage 

# pellet) Heat inpue A 

# = last firing chamber MCF/h 3 

# Hourly average B 

# =first firing chamber C 

# =preheat burners 

# Stack gas flow rate dscfm 4 

# continuous monitoring of gas Hourly average flow rate (test company) 

# Combustion zone degrees F Hourly average 

# temperature Fuel type 

# -- 

# -- Unusual production events 

# -- As needed 

# Ambient temperature degrees F Hourly average 1 

# L TPH (Long tons per hour) are an average for the 8-hour shift 2 

# Limited history on A 

# & B lower burners 3 

# MCF/hr (standard cubic feet of gas burned per hour), at 1000 Btu/scf 4 

# dscfm (dry standard cubic feet per minute) Flow rate is not readily adjustable 

# Range 100% Flux 61-63 estimated

310-370
A: TBD B:TBD C:TBD A -130,000-165,000 B -126,000-156,000 C -105,000-164,000 D-128,000-162,000 TBD Natural Gas



# --

--

2

# Process Emissions Control Devices Control equipment Control Manufacturer Monitored parameters 

# 10 equipment Model 

# (hourly averages) nomenclature CE014, CE015, Venturi scrubbers 

# Environeering Scrubber pressure drop, in. w.c. CE016, CE017 

# A33 (inches water column) Scrubber water flow, gpm (gallons per minute) Scrubber liquid maintained above pH 7 to pH 9 1 

# pH of scrubber liqUid will be measured at approximately 15 minute Intervals dunng the test


# Part IV: 

# Test Methods 

# All tests will be performed using the following USEPA reference test methods.

All test methods and are found In 

# 40 CFR 60 Appendix A 

# Pollutant, Test Method' parameter SOx, Method 1 Sample and Velocity Traverses for Stationary Sources. Twelvevolumetric point traverse for selecting representative point for continuous air flow rate, monitoring temperature Method 

# 2 Determination of Stack Gas Velocity and Volumetric Flow Rate. and moisture An US" type pitot tube fixed at a representative point in each stack. Differential pressure recorded with one minute and one hour averages in inches of water. Stack temperature using a type K thermocouple, recorded with one minute and one hour averages in 

# of. Method 3A Determination of Oxygen and Carbon Dioxide Concentrations in Emissions from Stationary Sources. A calibrated analyzer will be used to check the oxygen and carbon dioxide levels daily. The analyzer will continuously record from one of the sources and will be used as an indicator of significant change in the oxygen and carbon dioxide concentrations. Method 4 Determination of Moisture Content in Stack Gases. Daily wet bulb/dry bulb readings will be taken. In the event the sources are consistently saturated, further moisture calculations will assume saturation at the average stack temperature. Method 6C Determination of Sulfur Dioxide Emissions from Stationary Sources. The measurement of S02 concentration will be performed simultaneously at all four stacks following EPA Method 6C. The method performance will be modified by collecting data over up to 150 hours of representative plant operation. All analyzers will be calibrated initially for linearity and daily for zero and span checks. Data will be considered to be valid it drift is within the limits for a normal CEM system. Instruments will read PPM dry. 1



# 3 Process Emissions Control Devices Control equipment Control Manufacturer Monitored parameters 

# 10 equipment nomenclature Model 

# (hourly averages) CE014, CE015, Venturi scrubbers 

# En vironeering Scrubber pressure drop, in. w.c. CE016, CE017 

# A33 (inches water column) Scrubber water flow, gpm (gallons per minute) Scrubber liquid maintained above pH 7 to pH 9 1 

# pH of scrubber liqUid will be measured at approximately 15 minute Intervals dunng the test


# Part IV: 

# Test Methods 

# All tests will be performed using the following USEPA reference test methods.

Pollutant, Test Method 1 

# parameter SOx, Method 1 Sample and Velocity Traverses for Stationary Sources. Twelvevolumetric point traverse for selecting representative point for continuous air flow rate, monitoring temperature Method 

# 2 Determination of Stack Gas Velocity and Volumetric Flow Rate. and moisture An US" type pitot tube fixed at a representative point in each stack. Differential pressure recorded with one minute and one hour averages in inches of water. Stack temperature using a type K thermocouple, recorded with one minute and one hour averages in 

# of. Method 3A Determination of Oxygen and Carbon Dioxide Concentrations in Emissions from Stationary Sources. A calibrated analyzer will be used to check the oxygen and carbon dioxide levels daily. The analyzer will continuously record from one of the sources and will be used as an indicator of significant change in the oxygen and carbon dioxide concentrations. Method 4 Determination of Moisture Content in Stack Gases. Daily wet bulb/dry bulb readings will be taken. In the event the sources are consistently saturated, further moisture calculations will assume saturation at the average stack temperature. Method 6C Determination of Sulfur Dioxide Emissions from Stationary Sources. The measurement of S02 concentration will be performed simultaneously at all four stacks following EPA Method 6C. The method performance will be modified by collecting data over up to 150 hours of representative plant operation. All analyzers will be calibrated initially for linearity and daily for zero and span checks. Data will be considered to be valid it drift is within the limits for a normal CEM system. Instruments will read PPM dry. 1 

# All test methods and are found In 

# 40 CFR 60 Appendix A



# 3

# Part V: Continuous Emissions Monitors There are no continuous emissions monitors installed on the sources to be tested. 

# Part VI: Other Test Dates: March 11 through March 18,2008. The proposed test schedule follows': Monday Tuesday Wednesday Thursday Friday March 10 March 11 March 12 March 13 March 14 Setup day Begin sampling 24 hours of SOx 24 hours of SOx 24 hours of SOx at -12:00 p.m. data collection data collection data collection

The test schedule may be modified pnor to the test dates. Testing may be extended due to process upsets, test equipment failure or prolonged daily calibrations. 

# Saturday Sunday Monday Tuesday Wednesday March 15 March 16 March 17 March 18 March 19 24 hours of SOx 24 hours of SOx 24 hours of SOx Complete testing Contingency

data collection data collection data collection at 150 hours of data collection I


# Arcelor Mittal and Barr Engineering contacts will make themselves available for a pretest meeting prior to March 3. At the preference of the MPCA, ArcelorMittal suggests the pretest meeting be conducted by telephone. 

# Maintenance: A description of any necessary work done within 30 days prior to the test and the normal maintenance schedule followed will be included in the test report. 

# Test Reports: One hard copy of the test report will be submitted to the MPCA. ArcelorMittal requests that the required test report submittal be extended to 60 days following test completion because of the large volume of data to be processed and summarized. SOx emissions concentration data and calculated emissions rates will be submitted on CD-ROM in a nonprotected spreadsheet format (Excel). 

# Test plans and report submittals will be addressed to: Andrew Place Performance Test Coordinator Compliance and Enforcement Section-Industrial Division Minnesota Pollution Control Agency 520 Lafayette Road St. Paul, MN 55155-4194



# 4 Part V: Continuous Emissions Monitors There are no continuous emissions monitors installed on the sources to be tested.


# Part VI: Other Test Dates: March 11 through March 18,2008. The proposed test schedule follows!: Monday Tuesday Wednesday Thursday Friday March 10 March 11 March 12 March 13 March 14 Setup day Begin sampling 24 hours of SOx 24 hours of SOx 24 hours of SOx at -12:00 p.m. data collection data collection data collection Saturday Sunday Monday Tuesday Wednesday March 15 March 16 March 17 March 18 March 19 24 hours of SOx 24 hours of SOx 24 hours of SOx Complete testing Contingency

data collection data collection data collection at 150 hours of data collection I 

# The test schedule may be modified pnor to the test dates. Testing may be extended due to process upsets, test equipment failure or prolonged daily calibrations. 

# Arcelor Mittal and Barr Engineering contacts will make themselves available for a pretest meeting prior to March 3. At the preference of the MPCA, ArcelorMittal suggests the pretest meeting be conducted by telephone. 

# Maintenance: A description of any necessary work done within 30 days prior to the test and the normal maintenance schedule followed will be included in the test report. 

# Test Reports: One hard copy of the test report will be submitted to the MPCA. ArcelorMittal requests that the required test report submittal be extended to 60 days following test completion because of the large volume of data to be processed and summarized. SOx emissions concentration data and calculated emissions rates will be submitted on CD-ROM in a nonprotected spreadsheet format (Excel). 

# Test plans and report submittals will be addressed to: Andrew Place Performance Test Coordinator Compliance and Enforcement Section-Industrial Division Minnesota Pollution Control Agency 520 Lafayette Road St. Paul, MN 55155-4194



# 4

# Closing Remarks If there are questions or comments about the information provided, please contact me by telephone or e-mail.

Jaime Baggenstoss Environmental Engineer ArcelorMittal Minorca Mine Attachments: Figure 1 SV014-SV017--drawing c: Richard Berg-Barr Engineering Company



# 5 Closing Remarks If there are questions or comments about the information provided, please contact me by telephone or e-mail.

Jaime Baggenstoss Environmental Engineer ArcelorMittal Minorca Mine Attachments: Figure 1 SV014-SV017--drawing c: Richard Berg-Barr Engineering Company



# 5

# AppendixH Project Participants 

# AppendixH Project Participants

# Project Participants and Contact Information
ArcelorMittal Minorca Mine, Inc. Jaime Baggenstoss

- Environmental Engineer Jon Maki - Process Engineer Mike Long - Corporate Environmental Engineer 

# Barr Engineering Company Tim Russell - Vice President/Chemical Engineer Tom Kuchinski

- Stack Testing Supervisor Pete Rossmiller

- Senior Air Quality Technician Aaron Aamold

- Stack Test Technician Tom Leier

- Stack Test Technician Richard Berg - Senior Air Quality Technician/Project Manager 

# CONTACT INFORMATION ArcelorMittal 

# Minorca Mine Jaime Baggenstoss Environmental Engineer ArcelorMittal Minorca Mine, Inc. P.O. Box I 

# 5950 Old 

# Hwy 53 Virginia, MN 55792 (218) 749-5910 ext. 283 (218) 749-5256 jaime.baqqenstoss@arcelormittal.com

#2369C06003 

# Barr Engineering Co. Richard Berg Sr. Air Quality Technician Barr Engineering Company 4700 W. 77 Street Minneapolis, 

# MN 55435 (952) 832-2787 (952) 832-260 I 

# fax rberg@barr.com 

# Project Participants and Contact Information
ArcelorMittal Minorca Mine, Inc. Jaime Baggenstoss

- Environmental Engineer Jon Maki

- Process Engineer Mike Long

- Corporate Environmental Engineer 

# Barr Engineering Company Tim Russell

- Vice President/Chemical Engineer Tom Kuchinski

- Stack Testing Supervisor Pete Rossmiller

- Senior Air Quality Technician Aaron Aamold

- Stack Test Technician Tom Leier

- Stack Test Technician Richard Berg

- Senior Air Quality Technician/Project Manager 

# CONTACT INFORMATION ArcelorMittal Minorca Mine Jaime Baggenstoss Environmental Engineer ArcelorMittal Minorca Mine, Inc. P.O. Box 1 5950 Old 

# Hwy 53 Virginia, MN 55792 (218) 749-5910 ext. 283 (218) 749-5256 jaime.baqqenstoss@arcelormittal.com

#2369C06003 

# Barr Engineering Co. Richard Berg Sr. Air Quality Technician Barr Engineering Company 4700 W. 77 Street Minneapolis, 

# MN 55435 (952) 832-2787 (952) 832-260 I 

# fax rberg@barr.com